United States Office of
Environmental Protection Emergency and
Agency Remedial Response
EPA/ROD/R08-91/054
January 1991
EPA Superfund
Record of Decision:
Rocky Flats Plant (USDOE),
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50272-101
REPORT DOCUMENTATION 11. REPORTNO. 12.
PAGE EPA/ROD/R08-91/054
3. RecIpients Acceasion No.
4. TI1Ie and Subtitle
SUPERFUND RECORD OF DECISION
Rocky Flats Plant (USDOE), CO
Second Remedial Action
7. Author(s)
s. Report Date
01/25/91
&.
a
8. Perfonning Organization Rept. No.
9. Perfonning Orgainizalion Name and Acldreu
10. Projec1lTaaklWork Unit No.
.']a
11. ContraC1(C) or Grant(G) No.
(C)
(G)
12. Sponsoring Organization Name and Addreaa
U.S. Environmental Protection
401 M Street, S.W.
Washington, D.C. 20460
13. Type of Report & Period Covered
Agency
800/000
14.
15. Supplementary Notes
1&. Abstract(Umit: 200 words)
The 450-acre Atlas Mine Area is part of the Atlas Asbestos Mine site in Fresno
County, California. The site consists of four geographically distinct areas (the
Atlas Mine Area, the Clear Creek Management Area (CCMA), the Ponding Basin of the
California Aqueduct, and the City of Coalinga). The Atlas Mine Area is on rural land
owned by the Federal government and private parties, and surrounding land is used for
mining, ranching, farming, and recreation. The Mine Area includes three open pit
asbestos mine surfaces, stockpiles of asbestos waste material, an abandoned mill
building, a settling pond, and debris. Construction of an asbestos mill at the Atlas
Mine began in 1962, and onsite asbestos mining and milling activities occured from
1967 to 1979. Approximately three million cubic yards of asbestos ore and asbestos
mill tailings from onsite operations were bulldozed into piles adjacent to the mill
building. In 1976 and 1980, the Atlas Mine was cited for violating asbestos
emissions standards. In early 1980, after detecting elevated levels of asbestos in
water samples from the California Aqueduct, the State concluded that additional
corrective measures were necessary to prevent mine- and mill-generated asbestos from
entering the drainage basins. Further State investigations identified high
(See Attached Page)
17. Document Ana/y8is .. Deacrlptora
Record of Decision - Rocky Flats Plant (USDOE), CO
Second Remedial Action
Contaminated Medium: sw
Key Contaminants: VOCs (carbon tetrachloride, PCE, TCE), radioactive materials
b. IdentifierslOpen-Ended Tenns
Co COSA 11 ReId/Group
18. Availability Statement
19. Sec:uri1y CI... (This Report)
None
20. Sec:uri1y Clasa (This Page)
Non~
21. No. of Pages
578
22. Price
(See ANSI-Z39.18)
See InslnJctjollll on ,.-
272 (4-77)
(Formerly NTl5-3S)
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EPA/ROD/R08-91/054
Rocky Flats Plant (USDOE), CO
Second Remedial Action
Abstract (Continued)
.
~
concentrations of asbestos in the Mine Area soil, surface water, and air. A 1989
Record of Decision (ROD) for the City of Coalinga Operable Unit addressed cleanup of
asbestos-contaminated soil in Coalinga, California by burying the contaminated material
in a waste management unit with an impermeable cap. This ROD is designed to control
the release of asbestos from the Mine Area. No actions are proposed at this time for
the CCMA or the Ponding Basin of the California Aqueduct. In 1992, EPA will evaluate
the Department of Interior Bureau of Land Management's revised land use plan for CCMA
to determine if the plan is adequate to minimize airborne asbestos emissions, and the
U.S. Bureau of Reclamation and California Department of Waste Resources actions to
minimize airborne emissions from the Ponding Basin to determine if further action is
necessary. Tqe primary contaminant of concern affecting the soil, sediment, debris,
surface water, and air is asbestos, an inorganic.
The selected remedial action for this site includes paving the road through the Mine
Area or implementing an appropriate road maintenance alternative; constructing stream
diversions, sediment trapping dams, and other slope stabilization elements; instituting
a verification sampling plan involving surface water modeling and surface water and
stream bed sampling, as necessary; conducting a revegetation pilot project, and
implementing revegetation if found to be technically feasible and cost-effective;
dismantling the mill building with offsite disposal along with other debris from the
Mine Area; and implementing institutional controls including deed and land use
restrictions, and site access restrictions such as fencing. The estimated present
worth cost for this remedial action is $4,286,000, which includes an annual O&M cost of
$19,000.
PERFORMANCE STANDARDS OR GOALS: All diversion and drainage facilities will be designed
and constructed to accommodate the anticipated volume of precipitation and peak flows
from surface runoff in a 25-year, 24 hour storm. All tailings will be protected from
100-year peak stream flows. Quantification of risk reduction is difficult because
asbestos from natural and disturbed areas will continue to enter the surface water;
however, a verification sampling plan will be implemented to confirm that an
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. .~ .~~~~;~
,1 ;~
.
DOE EA - 0496
.It
FINAL
SURFACE WATER
INTERIM MEASURESI
INTERIM REMEDIAL ACTION PLAN I
ENVIRONMENTAL ASSESSMENT
AND DECISION DOCUMENT
SOUTH WALNUT CREEK BASIN
OPERABLE UNIT NO.2
u.s. DEPARTMENT OF ENERGY
Rocky Rats Plant .
Golden, Colorado'
. ENVIRONMENTAL RESTORATION PROGRAM
8 March 1991
-------
DOE/EA - 0496
.
,.,.
SURFACE WATER INTERIM MEASURES/INTERIM REMEDIAL ACTION PLAN/
ENVIRONMENTAL ASSESSMENT AND DECISION DOCUMENT
SOUTH WALNUT CREEK BASIN
OPERABLE UNIT NO.2
VOLUME I
U.S. Department of Energy
Rocky Flats Plant
Golden, Colorado
8 MARCH 1991
FINAL
Prepared by:
EG&G Rocky Flats. Inc.
Rocky Flats Plant
Golden, Colorado 80401
REVIEWED FOR CLASSIFICATION/UCNI
By F. J. Curran
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.
.
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EXECUTIVE SUMMARY
.
Water quality investigations have identified the presence of volatile organic compound (VOC) and
radionuclide contamination of surface water at the Rocky Flats Plant (RFP).
The subject Interim
"
Measures/Interim Remedial Action Plan/Environmental Assessment (IM/IRAP /EA) addresses contaminated
surface water in a portion of the South Wainut Creek drainage basin located within an area identified as
Operable Unit No.2 (OU 2). There is no immediate threat to public heaith and the environment posed by this
surface water contamination. The affected surface water is contained within the plant boundary by existing
detention ponds, and is treated prior to discharge for removal of voiatUe contaminants and suspended
particulates to which radionuclides, if present. are likely to adsorb. However, there is a potential threat and
the Department of Energy (DOE) is implementing this Surface Water 1M/I RAP at the request of the U.S.
Environmental Protection Agency (EPA) and Colorado Department of Health (CDH). Implementation of the
Surface Water 1M/IRA will enhance the DOE's efforts towards containing and managing contaminated surface
water, and will mitigate downgradient migration of contaminants. Another factor in implementing this 1M/IRA
is the length of time it will take to complete the investigations and engineering studies necessary to determine
the finai remedy for OU 2.
In February and March 1990, representatives from DOE, EPA. and CDH met to discuss surface water
IM/IRAs at the RFP site. The resutt of these meetings was a series of agreements, with the concurrence of
all parties. to implement an 1M/IRA for the cleanup of contaminated surface water in OU 2. OU 2 is defined
- .-
in the Environmentai Restoration Federal Facility Agreement and Consent Order (commonly known as the
"Inter-Agency Agreernenr or lAG). and is comprised of several Individual Hazardous Substance Sites (IHSSs)
that were formerly known in aggregate as the 903 Pad, Mound. and East Trenches Areas.
On 26 September 1990, the DOE released for public comment a proposed Surface Water 1M/IRA Plan
and Decision Document for OU 2. In this Plan, specific point source locations in the South Walnut Creek and
Woman Creek drainage basins were proposed for collection of surface water. According to the Plan, surface
water collected in each basin was to be transferred to a treatment facility discharging to the South Walnut
FINAl. SU~FACE WATE~ INTE~I/ol FU;/oIEOIAI. AC'T1ON P\.AN
~KY Fi..ATS Puo."''T. GO~"'. COLOIlAOO
891.. .~lrap\..,I'\Ut ..DUITI.mat
M&rC~ ~9S'
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Creek drainage. Comments on the 1M/IRA Plan received during the public comment period. however. revealed
strong opposition to the transfer of radionuclide contaminated seep water from the Woman Creek drainage
.
to the South Walnut Creek drainage.
Opposition was based on the absence of a proven perlormance record for the proposed 1M/IRA
..
treatment facility with respect to radionuclide removal and the potential for treatment process upsets. In
addition. the public voiced strong concern over potential worker and public health risks resulting from
construction activities In the Woman Creek Basin (i.e., atmospheric suspension of radlonuclide-contaminated
dust). In light of these concerns. the DOe and regulatory agencies agreed to eliminate the proposed interbasin
transfer of surface water seeps within this 1M/IRA Plan and to collect and treat Woman Creek seepage under
a separate OU 21M/IRA project. It is expected that the Surface Water 1M/IRA Plan for Woman Creek Basin
can be completed during the summer of 1991. This wUI allow adequate time to conduct bench-scale treatability
studies of radionuclide removal treatment processes. The results of the bench-scale studies will provide a
better assessment of applicable treatment technologies in selection of the preferred 1M/IRA alternative for the
Woman Creek Basin.
The Surface Water 1M/IRA Plan dated 26 September 1990 has thus been modified to focus on collection
and treatment of South Walnut Creek Basin contaminated surlace water. The Plan presented in this document
reflects this modification. In addition to previous consideration of collection of surlace water at stations SW-59
and SW~1. this Plan also proposes collection at a third location designated as SW-132. SW-132 represents
the discharge of a buried. corrugated metal culvert approximately 22S feet downgradient of SW~1. Recent
field surveys and review of as-built site drainage drawings have identified the culvert to be a conduit for flow
from the upper reach of South Walnut Creek within the Perimeter Security Zone (PSZ). Although water quality
data are not available at this newty designated station. its character is expected to be similar to the flow at SW-
61. A flow monitoring and sampling program has recently been initiated at SW-132. This South Walnut Creek
Basin 1M/IRA Plan provides for the collection of all flow from SW-S9. SW~1. and SW-132. except during
infrequent high flow periods resulting from high precipitation events. As discussed herein. the South Walnut
~INAl S:.JR~ACE WATER INTERIIoI REIoIEDIAl ACTION PLAN
=lQC1(V ":..ATS !>;.AN-. GO:..DE"-. COlORAOO
89&; ""'~&Q .'IIItI8lnioll.."uf"P'I.tna1
"'.fC" 199'
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Creek Basin 1M/IRA design flow is SO gallons per minute (gpm). The average annual flow rate from SW-S9.
SW~1. and SW-132 should be less than 20 gpm, however.
.
This 1M/IRA will be conducted in accordance with the Resource Conservation and Recovery Act of 1976
(RCRA), as amended by the Hazardous and Solid Waste Amendments of 1984 (HSWA); the Comprehensive
Environmental Response. Compensation, and liability Act of 1980 (CERCLA), as amended by the Superfund
Amendments and Reauthorization Act of 1986, the National Environmental Policy Act (NEPA) of 1969; and DOE
NEPA guidelines (52 FR 47662-47670. December 1987). DOE and EG&G have prepared this IM/IRAP /EA to
identify and evaluate interim remedial action alternatives for contaminated surface water in the South Walnut
Creek drainage basin. Based on the evaluations, a preferred surface water collection and treatment system
is recommended.
DOE will implement this 1M/IRA while work progresses on the RCRA Facility
Investigation/CERCLA Remedial Investigation (RFI/RI) and RCRA Corrective Measures Study/CERCLA
FeasibUIty Study (CMS/FS) for OU 2.
Having presented the general extent of the contamination within the South Walnut Creek Basin and the
specific environmental issues associated with surface water contamination, this plan subsequently presents an
evaluation of the remedial alternatives with respect to effectiveness. implementability, and costs. Effectiveness
includes abUity to meet Applicable or Relevant and Appropriate Requirements (ARARs). It must be noted.
however. that in accordance with the National Contingency Plan (NCP) and the lAG. IM/IRAs need only attain
ARARs to the greatest extent practicable.
Surface water will be collected at one seep and at two in-stream locations on South Walnut Creek
upstream of the existing detention ponds. This will reduce the potential for further downstream contamination.
Screening of surface water treatment technologies includes evaluation of: suspended solids, radionuclides.
and metals removal by chemical treatment/cross-flow filtration. granular media filtration, and ion exchange. and
evaluation of volatile organic contaminant removal by granular activated carbon (GAC) adsorption. ultraviolet
peroxide oxidation, and air stripping with off-gas treatment. The chemical precipitation/cross-flow membrane
filtration system. together with a GAC adsorption system. is selected as the preferred alternative. Laboratory
~II'iAl. SU"!~ACI: WATE"! I~O!1M O!EMEOIAI. ACi1OI'i F'U\1'i
O!OC>(V ~:...ATS ~..A'" GO\..OEN. ::oLOFlAOO
819&; ....trloQ .,..,nut 8uurn.1"\8I
~&fC:1'\ 199"
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and field treatability studies are being implemented in order to verify the performance of the selected
alternative. The current schedule for the field treatability studies calls for installation of a pilot system by Spring
1991. The field treatability unit will be operated to evaluate performance against chemical-specific ARARs. The
.
results may indicate that it is not practicable to attain all ARARs for the Surface Water 1M/IRA. Final
performance requirements for the 1M/IRA will require approval by the regulatory agencies. An additional
.,
function of the field treatability unit is the characterization and quantification of residuals generated by the
treatment processes being operated. thus allowing confirmation or modification of assumptions made in this
1M/IRA PI~n regarding the nature of treatment residuals. Table 0-1. Appendix D. shows the mUestone schedule
for the South Walnut Creek Basin Surface Water 1M/IRA project.
The IM/IRAP /EA examines the environmental and health risks associated with each of the alternatives,
including the preferred alternative. in accordance with the requirements of NEPA. The results of this evaluation
illustrate that the potential negative impacts to air and water quality, land. and short- and long-term land
productivity, as well as exposure of personnel. are minimal compared to the benefits of the resulting water
quality improvements to the surface waters of the area.
FItoW. SURFACE WATEFlINTERlM REMEOlAL ACTION PLAN
~>
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'"
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.
SECTION
'8
2
TABLE OF CONTENTS
TITLE
PAGE
EXECUTIVE SUMMARY. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. EX- 1
INTRODUCTION. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ., 1-1
1.1
Background. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 1 -3
1.2
1M/IRA Plan Organization. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 1-4
SITE CHARACTERIZATION. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-1
2.1
Site Description and Background. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-1
2.1.1 Location and Facility Type ...............,................. 2-1
2.1.2 Operable Unit 2 Description. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-3
2.1.2.1 903 Pad Area. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-3
2.1.2.2 Mound Area. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-5
2.1.2.3 East Trenches Area. . .. . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2~
2.1.3 Surrounding Land Use and Population Density. . . . . . . . . . . . . . . . .. 2-7
2.2
Affected and Sensitive Environment. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-9
2.2.1 Physical Environment. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-9
2.2.2 Regional and Local Hydrogeology. . . . . . . . . . . . . . . . . . . . . . . . . .. 2-11
2.2.2.1 Alluvial Materials. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-11
2.2.2.2 Bedrock Materials. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2- 15
2.2.3 Site Hydrology. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2- 17
2.2.3.1 Surface Water. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-17
2.2.3.2 Ground Water. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-19
2.2.4 Ecology.............................................. 2-22
2.2.5 Sensitive Environments and Endangered Species. . . . . . . . . . . . . . .. 2-23
2.2.6 Wetlands............................................. 2-24
2.2.1 Historic Sites. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2.25
2.3
Contaminants - Description and Sources. . . . . . . . . . . . . . . . . . . . . . . . . .. 2-25
2.3.1 Background Characterization. . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-25
- 2.3.2 Ground-Water Contamination. . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2.26
2.3.2.1 Volatile Organic Contamination. . . . . . . . . . . . . . . . . . . . . .. 2-26
2.3.2.2 Inorganic Contamination. . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-27
2.3.3 SoD Contamination. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-31
2.3.4 Sediment Contamination. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-34
2.3.4.1 Woman Creek Drainage. . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-34
2.3.4.2 South Walnut Creek Drainage. . . . . . . . . . . . . . . . . . . . . . .. 2-36
2.3.5 Surface Water Contamination. . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-37
2.3.5.1 Surface Water Stations Southeast of
903 Pad Area. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-38
2.3.5.2 Upper South Walnut Creek. . . . . . . . . . . . . . . . . . . . . . . . .. 2-40
2.3.5.3 Seeps at the East Trenches Areas. . . . . . . . . . . . . . . . . . . .. 2-41
2.3.6 Air Contamination. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-41
2.3.7 Summary of Contamination. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-42
molAl. SUI'!F4CE W4TEI'! IN'TEFlJIoI I'!EMEOIAI. 4~ PLAN
"lOCI('( F:,ATS "I.AJ'r.. GOL.DE.... COLOR4OO
.gA; "lr&g.~nlJ1 mar.tOl:.""8:
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SECTION
3
4
TABLE OF CONTENTS (continued)
.!!IL&
PAGE
.
2.4
Analytical Data. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-42
Site Conditions That Justify an IRA .......................... 2-43
"
2.5
IDENTIFICATION OF INTERIM REMEDIAL ACTION OBJECTIVES. . . . . . . . . . . . . . .. 3-1
3.1
Scope of Interim Measures/Interim Remedial Action. . . . . . . . . . . . . . . . . . .. 3-1
3.2
Interim Remedial Action Schedule. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 3.1
3.3
Compliance with Applicable or Relevant and Appropriate
Requirements (ARARs) and Protection of Human Health and
the Environment. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 3-1
3.3.1 Ambient or Chemical-Specific Requirements. . . . . . . . . . . . . . . . . . .. 3-3
3.3.1.1 Safe Drinking Water Act Maximum Contaminant
Levels (MCLs) and MCL Goals. . . . . . . . . . . . . . . . . . . . . . .. 3-4
3.3.1.2 Ambient Water Ouallty Criteria. . . . . . . . . . . . . . . . . . . . . . . .. 3-5
3.3.1.3 Colorado Surface and Ground.Water
Ouallty Standards. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 3-5
3.3.1.4 RCRA Ground-Water Protection Standards. . . . . . . . . . . . . . .. 3~
3.3.1.5 Protection of Human Health and the Environment. . . . . . . . .. 3- 7
3.3.2 Location-Specific Requirements. . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 3-7
3.3.3 Performance. Design, or Other Action-Specific
Requirements. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 3-8
IDENTIFICATION AND ANALYSIS OF 1M/IRA ALTERNATIVES. . . . . . . . . . . . . . . . .. 4-1
4.1
Surface Water Collection and Treatment Altematives . . . . . . . . . . . . . . . . . . .. 4-1
4.1.1 Surface Water Collection Technologies. . . . . . . . . . . . . . . . . . . . . . .. 4.2
4.1.2 Surface Water Treatment Technologies. . . . . . . . . . . . . . . . . . . . . . .. 4~
4.2
1M/IRA Alternative Evaluation Process. . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-9
- 4.-2.1 Effectiveness.......................................... 4-1 0
4.2.2 Implementabillty........................................ 4-10
4.2.3 Costs................................................ 4-10
4.3
Evaluation of the 1M/IRA Surface Water Collection System. . . . . . . . . . . . .. 4.11
4.3.1 Surface Water Collection by Diversion at the Sources. . . . . . . . . . .. 4-11
4.3.1.1 Description...................................... 4-11
4.3.1.2 Effectiveness.................................... 4-18
4.3.1.3 Implementabillty . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-20
4.3.1.4 Costs.......................................... 4-21
4.4
Evaluation of Surface Water Treatment Technologies. . . . . . . . . . . . . . . . . .. 4.21
4.4.1 Suspended Solids Removal. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-21
4.4.1.1 Cross-Flow Membrane Filtration. . . . . . . . . . . . . . . . . . . . .. 4.21
4.4.1.2 Granular Media Filtration. . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-30
.'N"'- SURF"CE W"TCR INTER!'" REr.lEOIAl AC110N PLAN
~I(V FloATS PLANT. GOlDEN. COl~OO
eg&g -"""8:). tfIII8.InUt . mat" 1OC.maI'
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.
SECTION
.
5
6
7
TABLE OF CONTENTS (continued)
TTTLE PAGE
4.4.2 RadionucJides and Metals Removal. . . . . . . . . . . . . . . . . . . . . . . . .. 4-34
4.4.2.1 Cross-A ow Membrane Filtration. . . . . . . . . . . . . . . . . . . . .. 4-34
4.4.2.2 Ion Exchange. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-38
4.4.3 Organic Contaminant Removal. . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-42
4.4.3.1 Activated Carbon Adsorption. . . . . . . . . . . . . . . . . . . . . . . .. 4-42
4.4.3.2 Ultraviolet (UV) Peroxide Oxidation. . . . . . . . . . . . . . . . . . .. 4-47
4.4.3.3 Air Stripping with Off-Gas Treatment. . . . . . . . . . . . . . . . . .. 4-55
COMPARATIVE ANALYSIS. . . . . . . . . . . . . . . . . . . .. . . . . . . . . . . . . . . . . . . . . . .. 5-'
5.1
Introduction. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 5-'
5.2
Comparison of Technologies. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 5.,
PROPOSED 1M/IRA. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-'
6.1
Summary. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-'
6.1.1 Surface Water Collection. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-1
6.1.2 Surface Water Treatment. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . , , .. 6-2
6.1.2.' Suspended Solids and Radionuclide Removal. . . . . . . . . . . .. 6-5
6.1.2.2 Organic Containment Removal. . . . . . . . . . . . . . . . . . . . . . .. 6-9
6.1.2.3 Effluent Discharge. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-9
6.2
Operation and Maintenance. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-' 0
6.2.1 Surface Water Collection. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-10
6.2.2 Cross-Flow Membrane Filtration. . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-10
6.2.3 Activated Carbon. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-11
6.3
Additional Documents. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-11
6.4
Treatability Studies. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 6-12
, ENVIRONMENTAL EFFECTS OF THE PROPOSED INTERIM REMEDIAL ACTION. . .. 7-1
7.1
Air Ouality . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7-'
7.2
Water Ouallty """"""""""..........................., 7-4
7.3
Terrestrial Impacts . . . . . . . . . . . . . . . . . . . . . . . . . . . . . , . . . . . . . . . . . . . .. 7-6
7.4
Archaeology and Historic Sites. . . . . . . . . . . . . . . . . . . . . . . . . . . . . , . . . . ., 7-8
7.5
Short- and Long-Term Land Productivity. . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7-8
7.6
Personnel Exposures - Analysis Methodology. . . . . . . . . . . . . . . . . . . . . . . .. 7-8
;&; ~'raQ' ...,n..."!' mar tOC.mar
Ma'c!'" ~9S'
-------
SECTION
8
9
APPENDIX A
Table A-1
Table A-2
Table A-3
Table A-4
. TABLE OF CONTENTS (continued)
TITLE PAGE
.
7.7
Personnel Exposures - Routine Operations. . . . . . . . . . . . . . . . . . . . . . . . .. 7 -11
7.7.1 Worker Exposure Risks. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7-11
7.7.2 Site Employee Exposure Risks. . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7-14
7.7.3 Risks from Exposure to Members of the Public. . . . . . . . . . . . . . . .. 7-16
.
7.8
Personnel Exposures - Accident. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7 -17
7.9
Commitment of Resources. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7 -18
7.10
Transportation Impacts. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7-18
7.11
Cumulative Impacts. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 7-21
ENVIRONMENTAL EFFECTS OF THE ALTERNATIVES. . . . . . . . . . . . . . . . . . . . . . .. 8-1
8.1
Environmental Effects of No Action. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 8- 1
8.1.1 Environmental Quality. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 8-1
8.1.2 Personnel Exposure. . . . . . . . . . . . . . . . . . . . . . . ': . . . . . . . . . . . . .. 8-2
8.1.3 Transportation.......................................... 8.2
8.2
Environmental Impacts of Alternative 2 . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 8.2
8.2.1 Environmental Quality. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 8-2
8.2.2 Personnel Exposure. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 8-3
8.2.3 Transportation.......................................... 8-3
8.3
Summary. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 8-3
REFERENCES. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 9.1
UST OF APPENDICES
Data Tables, Operable Unit NO.2
Background Ground-Water (Second Quarter 1989) Tolerance Interval Upper
Umits Maximum Detected Value
Background Surface Water (Second Quarter 1989) Tolerance Interval Upper
Umits or Maximum Detected Value
Background Sediment Tolerance Interval Upper Umits or Maximum Detected
Value February 1989
Background Geologic Materials Tolerance Interval Upper Umits Maximum
Detected Value 1989
~INAL. SURFACE WATER INTERIM REt.!EOIAI. ACT1O/II PLAN
~OCI(V "LA'rS ":..AN'" GOI.DEN. COI.ORAOO
e-;&; ......ra: .w&tnut' mar .toe.mar
o.A8I<" :9S'
-------
.
Table A-5
Table A-6
"
Table A-7
Table A-8
Table A-9
Table A-1Q
Table A-11
Table A-12
Table A-13
Table A-14
Table A-15
Table A-16
APPENDIX B
Appendix B-1
Appendix B-2
Appendix B-3
Appendix B-4
Appendix B-5
Appendix B-6
APPENDIX C
APPENDIX D
Table D-1
TABLE OF CONTENTS (continued)
Volatile Organic Compounds Detected in Unconfined Ground Water Second
Quarter 1989
Volatile Organic Compounds Detected In Ground-Water Maximum Concentrations
Dissolved Metals Above Background in Ground Water
Inorganics Above Background in Ground Water
Dissolved Radionuclides Above Background in Ground Water
Volatile Organic Compounds Detected In SoDs
Semi-Volatile Organic Compounds Detected in Soils
Total Metals Above Background in Soils
Total Radionuclides Above Background in Soils
Volatile Organic Compounds Detected in Sediments
T etal Metals Above Background Sediments
Total Radionuclides Above Background in Sediments
Surface Water Sampling Results. Operable Unit No.2
Volatile Organic Compounds
Dissolved Metals
Total Metals
Other Inorganic Compounds
Dissolved Radionuclides
Total Radionuclides
Surface Water Sampling Results, Summary Tables
Operable Unit NO.2
Milestone Schedule, Surface Water IM/IRAP /EA, South Walnut Creek Basin, Operable
Unit No.2'
Milestone Schedule, Surface Water IM/IRA/EA, South Walnut Creek Basin, Operable
Unit No.2
FINAL SURFACE WATER INTERIM REMEDIAl ACTlON PlAN
ROCKY FLATS PlANT, GOLDEN, COLORADO
89&9\ _irap\ walnul\ marl toe.mar
March 1991
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APPENDIX E
Table E-1.1
Table E-1.2
Table E-1.3
Table E-1.4
Table E-2.1
Table E-2.2
Table E-2.3
Table E-2.4
Table E:3
Table E-4
APPENDIX F
Table F-1
APPENDIX G
TABLE OF CONTENTS (continued)
ARAR Tables for Surface Water Contaminants
.
Chemical-Specific ARARs for Compounds and Elements Detected
Above Background in Surface Water at Operable Unit No.2
Chemical-5pecific ARARs for Compounds and Elements Detected
Above Background in Surface Water at Operable Unit No.2
,
Chemical-Specific ARARs for Compounds and Elements Detected
Above Background in Surface Water at Operable Unit NO.2
Chemical-Specific ARARs for Compounds and Elements Detected
Above Background in Surface Water at Operable Unit No.2
Analysis of Chemical-Specific ARARs Pertinent to Surface
Water Operable Unit No.2 1M/IRA Options
Analysis of Chemical-Specific ARARs Pertinent to Surface
Water Operable Unit NO.2 1M/IRA Options
Analysis of Chemical-Specific ARARs Pertinent to Surface
Water Operable Unit NO.2 1M/IRA Options
Analysis of Chemical-Specific ARARs Pertinent to Surface
Water Operable Unit No.2 1M/IRA Options
Analysis of Action-Specific ARARs for Remedial Actions at
Operable Unit NO.2
Analysis of Location-Specific ARARs for Remedial Actions at
Operable Unit No.2
Aow Weighted Maximum Concentration Calculation Spreadsheet
Aow Weighted Average and Maximum Concentrations
Risk Assessment Calculations
FIIoW. SU~ACE WA'Tt:~ IN'TERlIIoI REIIoIEOIAl. AC'I1ON P\..AN
~I(V =..,A':'S P\..AN'1'. GOLDEN. COI.OAAOO
.9&.9\~'f'8& .w&ln\Jt mat'toe.mar
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-------
.
FIGURE
2-1
.. 2.2
2-3
2-4
2-5
2-6
2-7
2-8
2-9
2-10
2-11
2.12
4-1
4-2
4-3
4-4
4-5
4-6
4.7
4-8
4-9
4-10
6-1
TABLE OF CONTENTS (continued)
UST OF FIGURES
.IJM
PAGE
Location of Rocky Flats Plant. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2.2
Remedial Investigation Areas and Individual Hazardous
Substance Sites. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-4
Land Use in the Vicinity of the Rocky Flats Plant. . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-8
Surface Water Drainage Patterns at Rocky Flats Plant. . . . . . . . . . . . . . . . . . . . . .. 2-12
Erosional Surfaces and Alluvial Deposits. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-13
Generalized Stratigraphic Section. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-14
Potentiometric Surface of Unconfined Ground-Water Row System. . . . . . . . . . . . .. 2-20
Operable Unit No.2 Carbon Tetrachloride Isopleths for the Unconfined
Ground-Water Row System. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-28
Operable Unit No.2 Tetrachloroethene Isopleths for the Unconfined
Ground-Water Row System. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2.29
Operable Unit No.2 Trichloroethene Isopleths for Unconfined
Ground Water Row. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-30
SoU Sampling Locations. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 2-32
Surface Water and Sediment Monitoring Stations. . . . . . . . . . . . . . . . . . . . . . . . . .. 2-35
South Walnut Creek Basin Surface Water Monitoring Stations. . . . . . . . . . . . . . . . . .. 4-3
DetaO Plan of Surface Water Stations SW-59. SW-60. SW-61.
SW-132. and SW-133 ................................................ 4-4
Location of Proposed Surface Water Collection and Treatment Facilities. . . . . . . . .. 4-12
Typical Surface Water Collection and Diversion System. . . . . . . . . . . . . . . . . . . . .. 4.19
Cross-Row Membrane Filtration System. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4.25
Granular Media Filtration Treatment Unit. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-31
Ion Exchange Treatment System. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-39
. Carbon Adsorption Treatment Unit. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-44
UV /Peroxide System. . . . . . . . . . . . . ; . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-49
Air Stripping Wrth Vapor and Uquid-Phase Carbon Adsorption. . . . . . . . . . . . . . . .. 4-55
Proposed 1M/IRA Treatment System Process Row Diagram. . . . . . . . . . . . . . . . . . " 6-3
~INAL SUI'!.ACE WATE~ INTEI'!IU I'IEI.4EOIAL ACTION PLAN
"lOCI('! ~LATS PLA~. GOL!>EIo;. COLOP.AOO
eg&; ,-...rac ...,nUf mar'.tOC.mar
~arcr- ~ 9S'
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TABLE OF CONTENTS (continued)
UST OF TABLES
.
TABLE
J]!J,.g
PAGE
4-1
Basis for Design of Surface Water Treatment Plant. . . . . . . . . . . . . . . . . . . . . . . . . .. 4- 7
~
4-2
Surface Water Flow Data for SW-59 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-13
4-3
Surface Water Flow Data for SW-61 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-14
4-4
Surface Water Flow Data for SW-6Q . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-16
4-5
Design Flows and Average Annual Withdrawal Rates for Surface Water Diversion
and Collection System. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-17
4-6
Assumed Costs for Surface Water Diversion and Collection Systems. . . . . . . . . . .. 4-22
4-7
Assumed Costs for Cross-Flow Membrane Filtration Process. . . . . . . . . . . . . . . . .. 4-28
4-8
Estimated Costs for Granular Media Filtration Treatment Unit. . . . . . . . . . . . . . . . .. 4-33
4-10
Assumed Costs for Ion Exchange Treatment System. . . . . . . . . . . . . . . . . . . . . . .. 4-43
Assumed Costs for Granular Activated Carbon Treatment System. . . . . . . . . . . . . .. 4-48
4-9
4-12
Assumed Costs for UV Peroxide Oxidation Treatment System. . : . . . . . . . . . . . . . .. 4-53
Assumed Costs for Air Stripping with Vapor and Uquid Phase
Granular Activated Carbon. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 4-58
4-11
5-1
Comparative Analysis of Technologies. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 5-2
8-1-A
Summary Comparison of Potential Impacts of Proposed Action and Altematives . . . .. 8-4
8-1-B
Summary Comparison of Potential Impacts of Proposed Action and AI1ematives . . . .. 8-5
~1NA1. SURFACE WATCR INTERIM REMEOtAL. ACTION PI.AN
"OCICV ~!..ATS Pl.6,P
-------
,.
ACRONYM
-- ACL
Am
ARAR
AWQC
BAT
BOAT
BDL
CAA
CCI.
CCR
CDH
CEARP
CEDE
CEO
CERCLA
CFR
CHa3
CMS/FS
CRDL
CRP
CS
(;}NA
1 ,1-DCA
1.2-DCA
1,1-DCE
1,2-DCE
d/m/g
DOE
DOT
DRCOG
EE/CA
EIS
TABLE OF CONTENTS (continued)
GLOSSARY OF ACRONYMS
MEANING
Alternate Concentration Umit
Americium
Applicable or Relevant and Appropriate Requirement
Ambient Water Ouallty Criteria
Best Available Technology
Best Demonstrated Available Technology
Below Detection Umits
aean Air Act
Carbon Tetrachloride
Colorado Code of Regulations
Colorado Department of Health
Comprehensive Environmental Assessment and Response Program
Committed Effective Dose Equivalent
Council of Environmental Quality
Comprehensive Environmental Response. Compensation, and Liability Act of 1980
Code of Federal Regulations
Chloroform
Corrective Measures Study/Feasibility Study
Contract Required Detection Umlt
Community Relations Plan
Collection System (for Surface Water)
-Clean Water Act
1,1-
-------
ACRONYM
EP
EPA
ER
ERHSPP
FEMA
FFACO -
FIFRA
FRP
FS
ft/ft
ft/yr
GAC
gal/#f/d
GOCO
GPM
GPM/ff
HEC
HS&E
HSWA
H202
IHSS
lAG
IDL
1M/IRA
I RAP /EA
IRIS
I
-------
.
..
ACRONYM
mg/kg
mg/I
M
MDA
NCP
NEMA -
NEPA
NPDES
ORP
OSA
OU2
PCE
pCi/g
pCi/kg
pCi/1
PEL
PL
POTW
PPB
PPCD
PPM
PSI
Pu
PWF
QA/QC
RAAMP
RCRA
RfD
RFI/RI
RFP
RI
SARA
SCFM
TABLE OF CONTENTS (continued)
GLOSSARY OF ACRONYMS
MEANING
Milligrams Per Kilogram
Milligrams Per liter
Molarity
Minimum Detectable Activity
National Contingency Plan
National Electrical Manufacturer's Association
National Environmental Policy Act of , 969
National Pollutant Discharge Elimination System
Oxidation Reduction Potential
Operational Safety Analysis
Operable Unit NO.2
T etrachloroethene
picoCuries per Gram
picoCuries per Kilogram
picoCuries per liter
Permissible Exposure Umlts
Public Law
Publicly Owned Treatment Works
Parts Per Billion
Plan for Prevention of Contaminant Dispersion
Parts Per Million
Pounds Per Square Inch
"'Plutonium
Present Worth Factor
Quality Assurance/Quality Control
Radioactive Ambient Air Monitoring Program
Resource Conservation and Recovery Act of , 976
Reference Dose
RCRA Facility Investigation/Remedial Investigation
Rocky Flats Plant
Remedial Investigation
Superfund Amendments and Reauthorization Act of , 986
Standard Cubic Feet Per Minute
"IPW. SU~ACE WATER Ir-ITEFliIoI REIoIEOIAI. ACTlON PU\N
~KV "i..ATS PI..AN7. GOLDEN. ::OLORADO
~&;.....,t8Q waln~ .mar.toc.mar
Ma.rc" ~;;.
-------
TABLE OF CONTENTS (continued)
GLOSSARY OF ACRONYMS .
ACRONYM MEANING
SDWA Safe Drinking Water Act
SSHSP Site-Specific Health and Safety Plan ~
SW Surface Water Monitoring Station
TBC To Be Considered
1,1,1-TCA 1,1,1- Trichloroethane
1,1,2-TCA- 1,1 ,2-Trichloroethane
TCE Trichloroethene
TDS Total Dissolved Solids
TOSCO The Oil Shale Company
TSCA Toxic Substances Control Act
U Uranium
UMTRA Uranium Mill Tailings Remedial Action
USFWS United States Fish and Wildlife Service
UV Ultraviolet
VOCs Volatile Organic Compounds
x/a Average Dispersion Coefficient
p Micro
pCl/ml Microcuries Per Milliliter
pg/I Micrograms Per Liter
pg/kg Micrograms Per K'dogram
~INAL SUR~ACE WATCR I,.r,'ERIM REMEOtAL. ACT10N PL.AN
RC)CI('( ~:.A1'S Pi.AJ',""!. GOL.DEN. C01..ORAOO
.; . .,........: WlJI'\~ m81~ 1OC.1"\af
Mar.-. '95.
-------
'.."". ,:~~~~~~~~~:-:;:;~~~~:~.;.;~.c .,. .~,. .
'<"':'''''''',;;,,~
Section 1
-------
SECTION 1
INTRODUCTION
.
Water quality investigations have identified the presence of volatile organic compound (VOC) and
...
radionuclide contamination of surface water at the Rocky Rats Plant (RFP).
The subject Interim
Measures/Interim Remedial Action Plan/Environmental Assessment QM/IRAP /EA) addresses contaminated
surface water in a portion of the South Walnut Creek drainage basin located within an area identified as
Operable Unit No.2 (OU 2). There is no immediate threat to public health and the environment posed by
surface water contamination because the affected surface water is contained within the plant boundary by
existing detection ponds, and is treated prior to discharge for removal of volatile organic contaminants and
suspended particulates to which radionuclides, if present, are likely to adsorb. However, there is a potential
threat and the Department of Energy (DOE) is implementing this Surface Water Interim Measures/Interim
Remedial Action (1M/IRA) at the request of U.S. Environmental Protection Agency (EPA) and Colorado
Department of Health (CDH). Implementation of the Surface Water 1M/IRA will enhance the DOE's efforts
towards containing and managing contaminated surface water, and will mitigate downgradient migration of
contaminants. Another factor in implementing this 1M/IRA is the length of time it will take to complete the
investigations and engineering studies necessary to determine the final remedy for OU 2.
In February and March 1990, representatives from DOE, EPA, and CDH met to discuss surface water
IM/IRAs at the RFP site. The result of these meetings was a series of agreements, with the general agreement
of all parties, to implement an 1M/IRA for the clean-up of contaminated surface water in the area designated
as OU 2. OU 2 is defined in the final Environmental Restoration Federal Facility Agreement and Consent Order
(FFACO) (DOE, 1991), commonly known as the Inter-Agency Agreement ~AG). and is comprised of several
Individual Hazardous Substance Sites (IHSSs) that were formeriy known in aggregate as the 903 Pad, Mound,
and East Trenches Areas.
On 26 September 1990, the DOE released for public comment a Surface Water 1M/IRA Plan and
Decision Document for OU 2. In this Plan, specific point source locations in the South Walnut Creek and
SURFACE WATER II'lTERlM REMEOtAl AcnON PLAN
ROCKY FLATS PLANT, GOlDEN, COlOAAOO
eg&g\_irap\walnllt\_.I,mar
Man:h 1991
-------
Woman Creek drainage basins were proposed for collection of surface water. According to the Plan, surface
water collected In each basin was to be transferred to a treatment facility discharging to the South Walnut
Creek drainage. Comments on the 1M/IRA Plan received during the public comment period. however, revealed
.
strong opposition to the transfer of radlonuclide contaminated seep water from the Woman Creek drainage
to the South Walnut Creek drainage.
~
Opposition was based on the absence of a proven performance record for the proposed 1M/IRA
treatmenUacDIty with respect to radionuclide removal and the potential for treatment process upsets. In
addition, the public voiced strong concern over potential worker and public health risks resulting from
construction activities In the Woman Creek Basin (Le., atmospheric suspension of radionuclide-contamlnated
dust). In light of these concerns, the DOE and regulatory agencies agreed to eliminate the proposed interbasin
transfer of surface water and to collect and treat Woman Creek seepage under a separate au 21M/IRA
project. It is expected that the Surface Water 1M/IRA Plan for Woman Creek Basin can be completed during
the summer of 1991. This will allow adequate time to conduct bench-scale treatability studies of radionuclide
removal treatment processes. The results of the bench-scale studies will provide a better assessment of
applicable treatment technologies in selection of the preferred 1M/IRA alternative for the Woman Creek Basin.
The Surface Water 1M/IRA dated 26 September 1990 has thus been modified to focus on collection and
treatment of South Walnut Creek Basin contaminated surface water. The Piar. oresented in this document
reflects this modification. In addition to previous consideration of collection of surface water at stations SW-59
- .-
and SW~1. this Plan also proposes collection at a third location designated as SW-132. SW-132 represents
the discharge of a buried, corrugated metal culvert approximately 225 feet downgradient of SW.Q1. Recent
field surveys and review of as-buit site drainage drawings have identified the culvert to be a conduit for flow
from the upper reach of South Walnut Creek within the Perimeter Security Zone (PSZ). Although water quality
data are not available at this newly designated station. Its character Is expected to be similar to the flow at
SW.Q1. A flow monitoring and sampling program has recently been Initiated at SW-132. This South Walnut
Creek Basin 1M/IRA Plan will provide for the collection of all flow from SW-59. SW.Q1, and SW-132 except
during infrequent high flow periods resulting from high precipitation events.
SURFAce WATER INTERIM REMEDW. ACT10N PI.AN
~I(V .LArs po..»;.. GO.DEN. co..ORADO
eg&;. ~rac ,-.nU1,.~,'.tn8f
MatC~ 1118'
-------
This 1M/IRA will be conducted in accordance with the Resource Conservation and Recovery Act of 1976
.
(RCRA) as amended by the Hazardous and Solid Waste Amendments of 1984 (HSWA), the Comprehensive
Environmental Response, Compensation, and Uability Act of 1980 (CERCLA) as amended by the Superfund
Amendments and Reauthorization Act of 1986 (SARA), the National Environmental Policy Act (NEPA) of 1969.
..
DOE and EG&G have prepared this 1M/IRA Plan to identify and evaluate interim remedial action alternatives
for contaminated surface water in the South Walnut Creek drainage basin. Based on the evaluations. a
preferred 1M/IRA for the contaminated surface water is recommended.
This 1M/IRA Plan has been prepared to conform with the requirements for an Engineering
Evaluation/Cost Analysis (EE/CA) as defined in the National Contingency Pian (NCP) (FR Vol. 55, No. 46.
8813; 40 CFR 3OO.415[b][4]). It also conforms to the NEPA of 1969. as implemented by regulations
promulgated by the President's CouncU on Environmental Ouallty (CEO) (40 CFR 1500-1508). and DOE
Guidelines (52 FR 47622-47670. December 15, 1987).
This finalized IM/IRAP document is also an EA. Although the 26 September 1990 proposed IM/IRAP
contained all the information and assessments to make it an EA, It had not been approved as an EA by DOE
Headquarters and therefore coUd not be labeled as an EA. However. in the Executive Summary of the
26 September 1990 proposed IM/iRAP, It was noted that once public comment was received and DOE
Headquarters approved the NEPA aspects of the document. it would become an integrated CERCLA/RCRA .
NEPA document QM/IRAP /EA).
1.1
BACKGROUND
In March 1987. a Phase I Remedial Investigation (RI) under the Environmental Restoration (ER) Program
(formerty known as the Comprehensive Environmental Assessment and Response Program (CEARP)] began
. at au 2. The investigation consisted of the preparation of detailed topographic maps, radiometric and organic
vapor screening surveys. surface geophysical surveys, a soii gas survey, a boring and well completion
program. soil sampling and ground and surface water sampling. Phase I field activities were completed at
SURF4ce W47EFlINTERIM FlEMEDW. 4CT1ON PLAN
FIOCOCV "i.ATS P.ANT. GOlDEN, co..ORAOO
eg&; ,M-tI'8D,..,nUf\MC-'.maI
Marc" '118'
-------
OU 2 during 1987, and a draft RI report was submitted to EPA and CDH on December 31, 1987 (Rockwell
International, 1987a). Phase I data did not allow adequate definition of the nature and extent of contamination
.
for the purpose of conducting a feasibility study of remedial alternatives pertaining to contaminated media.
A draft Phase /I RI Sampling Plan that presents the details and rationale for further field work to achieve this
objective was submitted to the regulatory agencies in June 1988 (Rockwell International, 1988a). This draft
sampling plan was subsequentty revised and submitted as a final Phase II RCRA Facility Investigation/Remedial
..
Investigation Feasibility Study (RFI/RIFS) sampling plan in April 1990 (EG&G, 1990a). The plan was approved
by EPA in. May 1990.
A draft 1M/IRA plan for contaminated ground water at OU 2 was submitted in December 1989 (Rockwell
International, 19898). The plan was prepared based on limited knowtedge of the nature and extent of ground-
water contamination. Regulatory agency review of the document determined that, although an 1M/IRA for
ground water is required by the 1989 Agreement In Principle between DOE and CDH, insufficient information
on the nature and extent of ground-water contamination exists at this time to pursue effective ground-water
remediation. In order to facilitate early evaluation of the need for an 1M/IRA for ground water at OU 2, the final
Phase /I RR/RIFS sampling plan incorporates a phased investigation approach. The plan was approved by
the regulatory agencies. The phased approach is to investigate alluvial and hydraulically connected bedrock
migration pathways first, and then to subsequently investigate ground-water contaminant sources. This will
allow planning, design, and Implementation of a ground-water 1M/IRA, if necessary, before completion of the
RFI/RI and Corrective Measures Study/Feasibility Study (CMS/FS) for OU 2.
1.2
1M liRA PLAN ORGANIZATION
Section 2 of this 1M/IRA Plan provides site characterization information on the RFP and. in particular,
au 2. The discussion presented Includes site characterization information for both the South Walnut Creek
Basin and the Woman Creek Basin at OU 2. Although this 1M/IRA Plan exclusively addresses the collection
and treatment of contaminated South Walnut Creek Basin surface waters, it is useful to examine the
characteristics of both basins. As discussed above. the collection and treatment of Woman Creek Basin seeps
SURFACE wATER INTERIM REr.IEOIAI. ACTON PlAN
~ -L,ATS PI.ANT. GOt..DE~. CO-OfW)O
.;'._.rw>._"111._.1.....,
M8ICI"I 1 99'
-------
at OU 2 wUI be addressed under a separate 1M/IRA Plan. The discussion presented in Section 2 describes
the potentially affected environment associated with the proposed 1M/IRA and the results of the previous
~
investigations at OU 2. The information included in Section 2 has been derived from the draft RI report and
final Phase II RFI/RIFS Sampling Plan.
~
Section 3 identifies the objectives of the South Walnut Creek Surface Water 1M/IRA. Applicable or
Relevant and Appropriate Requirements (ARARs) and applicable environmental regulations. The objectives and
ARARs define the criteria used to identify and evaluate 1M/IRA alternatives.
Section 4 identifies technically feasible 1M/IRA alternatives for the collection and treatment of
contaminated South Walnut Creek Basin surface water. The 1M/IRA alternatives selected address the
objectives presented in Section 3. The alternatives are evaluated based on effectiveness. implementability, and
cost criteria.
Section 5 summarizes the analysis performed in Section 4, and Section 6 presents the preferred 1M/IRA.
Bench and field treatability studies to evaluate the performance of the preferred 1M/IRA are also discussed in
Section 6.
Sections 7 and e specifically address NEPA requirements regarding an analysis of environmental
impacts associated with the preferred 1M/IRA and other 1M/IRA alternatives. respectively. This analysis Is
intended to provide sufficient Information to aid In a NEPA determination of environmental impacts of the
proposed 1M/IRA. The SCOpe of the analysis does not include evaluation of the existing operations at the RFP,
final remedial actions at OU 2 or subsequent remedial actions at other locations of the RFP. The environmental
impacts of plant operation were previously analyzed in the final Environmental Impact Statement (EIS) (DOE,
1980). NEPA documentation for final remedial actions at OU 2 and any other RFP remedial actions will be
provided in future documents.
SURFACE WA~ IIITERIM REMEDW. ACTION PI.AN
ROCKY FL.A TS F'\.AHT, GaDEN. COLOAACO
.9",""""" W81nut',I8C-'.mar
Marc" '89'
-------
Volume II of this 1M/IRA Plan contains au 2 surface water, sediment. ground-water, and soils chemistry
data as well as the South Walnut Creek Basin Surface Water 1M/IRA schedule and a tabulation of ARARs.
.,
..
SURF ACE WATER IN'TERIM AEMEOIAL AC'T1ON PI.AN
ROCKY Fi.ATS I>\.AHT. GOl!)EN, COlORAOO
.Q._~._n"'\_.,.rnar
Marcn 1881
-------
-------
SECTION 2
SITE CHARACTERIZATION
4it
2.1 SITE DESCRIPTION AND BACKGROUND
--
2.1.1 Location and Facilitv Tvoe
The RFP is located in northem Jefferson County, Colorado. approximately 16 miles northwest of
downtown Denver (Figure 2-1). The plant site consists of approximately 6.550 acres of federally-owned land
in Sections 1 through 4, and 9 through 15, of T2S. R70W, 6th principal meridian. Plant buildings are located
within an area of approximately 400 acres, known as the RFP security area. The security area is surrounded
by a buffer zone of approximately 6.150 acres.
The RFP is a govemment-owned. contractor-operated (GOCO) facility. It is part of a nationwide nuclear
weapons research, development. production and plutonium reprocessing complex administered by the Rocky
Flats Operations Office of the DOE. The operating contractor for the RFP is EG&G Rocky Flats, Inc. The
facility manufactures components for nuclear weapons and conducts plutonium reprocessing and has been
in operation since 1951. The RFP fabricates components from plutonium, uranium, beryllium, and stainless
steel. Historically, production activities have included metal fabrication. machining. and assembly. 80th
radioactive and nonradioactive wastes are generated in the process. Current waste handling practices involve
on-site and off.site recycling of hazardous materials and off-site disposal of solid radioactive materials at
another DOE facility.
The RFP is currently an interim status RCRA hazardous waste treatment/storage facility. In the past,
both storage and disposal of hazardous and radioactive wastes occurred at on-site locations. Preliminary
assessments conducted under Phase 1 of the Environmental Restoration (ER) Program identified some of the
past on-site storage and disposal locations as potential sources of environmental contamination.
SU~"ACE WATEP INTE~I~ Re~EDIAI. ACTION PI..AN
I'a:I(V "!.A,S P\.ANT. CiO\..OEN. CO'-~
eog&g ~II'UI' ..,nU't .MC-2.mar
MarcP'l '95'
-------
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2-1
Location of Rocky Flats Plant
SURFACE WATER INTERlIoI REIoIEDIAI. ACTION PLAN
ROC"'" FLATS PLA"''T, GOLDEN, COLORADO
e;&. """'1'8Q ,W8JnUf"'.uc-2.mat
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2.1 .2 acerable Unit 2 Descriction
\
au 2 is comprtsed of the 903 Pad and Up, Mound, and East Trenches Areas which are located east-
southeast of the RFP as shown In Figure 2.2. The Areas of au 2 lie within either the South Walnut Creek or
..
Woman Creek drainage basins. Although this 1M/IRA Plan exclusively addresses the collection and treatment
of contaminated South Walnut Creek Basin surface water, it is useful to examine the historical uses and
characteristics of all au 2 Areas. including the 903 Pad and Up Area which lies entirely within the Woman
Creek drainage basin.
Twenty sites. designated as IHSSs, lie within au 2: five in the 903 Pad Area. four in the Mound Area,
and 11 in the East Trenches Areas. The historical use of the au 2 IHSSs is discussed below.
2.1.2.1 903 Pad Area
F"lVe sites are located within the 903 Pad Area (Figure 2-2). These sites are:
903 Drum Storage Site (IHSS Ref. No. 112)
903 Up Site (IHSS Ref. No. 155)
Trench T~2 Site (IHSS Ref. No. 109)
Reactive Metal Destruction Site (IHSS Ref. No. 140)
Gas Detoxification Site (IHSS Ref. No. 183)
Presented below are brief descriptions of each. of these sites.
1.
903 Drum Storage Site (IHSS Ref. No. 112) - The site was used from 1958 to 1967 to store drums
containing radioactively contaminated. used machine cutting oil. The drums, some of which corroded
and leaked. contained oDs and solvents contaminated with plutonium or uranium. Most of the drums
contained lathe coolant consisting of mineral oil and carbon tetrachloride (CCI.) in varying proportions.
However. an unknown number of drums contained hydraulic oils. vacuum pump oils, trichloroethene
(TCE) , tetrachloroethene (PCE), silicone oils, and acetone (Rockwell International. 1987b).
Ethanolamine was also added to new drums after 1959 to reduce the drum corrosion rate. All drums
were removed by 1968.
Su~.CE wua~ INTERlr..I I'IEMEOIAL AC'T1ON PI.AN
-------
POND
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EXPLANATION
~ INDMDUAI. HAZARDOUS SUBSTANCE Sf!! (IHSS)
~ NIl) IHSS DESlGN.4.11ON
~
1..OCA11ON OF BMR£I.S DETERWINED BY
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Scale: 18 = 600'
0'
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300'
I
800'
I
CONTOUR IHTERVAl . 20'
u.s. DEPARTMENT Of ENERGY
Rocky Flats Plant
Golden, Colorado
OPERABLE UNIT NO.2
SURfACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
FIGURE 2-2
REMEDIAL INVESTIGATION AREAS
AND INDIVIDUAL HAZARDOUS
SUBSTANCE SITES
March, 1991
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.
After the drums were removed, efforts were made to scrape and move the plutonium-contaminated soil
into a relatively small area. cover it with fill material, and top it with an asphalt containment cover. This
remedial action was completed in November 1969. An estimated 5,000 gallons of liquid leaked into the
soil during use of the drum storage site. The liquid was estimated to contain 86 grams of plutonium
(Rockwellintem&tional, 1987b).
2.
903 Up Site (IHSS Ref. No. 155) - During drum removal and clean-up activities associated with the
903 Drum Storage Site, winds distributed plutonium beyond the pad to the south and east. Although
some plutonium-contaminated soils were removed, radioactive contamination is stHI present at the 903
Up Site in the surficial soils.
3.
Trench T-2 Site (IHSS Ref. No. 109) - This trench was used prior to 1968 for the disposal of sanitary
sewage sludge and flattened drums contaminated with uranium and plutonium.
4.
Reactive Metal Destruction Site (IHSS Ref. No. 140) - This site was used during the 1950s and 1960s
primarily for the destruction of lithium metal (DOE, 1986). Small quantities of other reactive metals
(sodium, calcium, and magnesium) and some solvents were also destroyed at this location (lIIsley,
1978).
5.
Gas Detoxification Site (lHSS 183) - Building 952, located south of the 903 Drum Storage Site, was
used to detoxify various bottled gases between June 1982 and August 1983.
A Phase I RI has been completed for these five sites. Phase II is planned for this fall.
2.1.2.2 Mound Area
The Mound Area is composed of four sites (Figure 2-2). These are:
Mound Site (IHSS Ref. No. 113)
Trench T-1 Site (IHSS Ref. No. 108)
01 Bum Pit NO.2 Site (IHSS Ref. No. 153)
Pallet Bum Site (IHSS Ref. No. 154)
These sites are described individually below.
1.
Mound Site (lHSS Ref. No. 113) - The Mound Site contained approximately 1,405 drums containing
primarily depleted uranium and plutonium contaminated lathe coolant. Some drums also contained
"Perclene" (Smith. 1975). Perclene was a brand name of tetrachloroethene (Sax and Lewis. 1987).
Some of the drummed wastes placed in the Mound Site were in solid form (Rockwellintemational.
1987b). Qeanup of the Mound Site was accomplished in 1970, and the materials removed were
packaged and shipped to an off.slte DOE facility as radioactive waste. Subsequent surficial soils
sampling in the vicinity of the excavated Mound Site indicated 0.8 to 112.5 disintegrations per minute
per gram (d/m/g) alpha activity. This radioactive contamination is thought to have come from the 903
Drum Storage Site via wind dispersion rather than from the Mound Site (Rockwellintemational, 1 987a).
SURFACE WA~ INTER" RE"EDIAL ACT10N !>\.AN
~I("( Fi..ATS PI.ANT. GO...DeN. CO-OAAOO
89Ag ""lr8.O ;~nut ,18C-2.""8t
MatC'" , 9& ~
-------
2.
Trench T-1 Site (IHSS Ref. No. 108) - The trench was used from 1954 untU 1962 and contains
approximately 125 drums filled with depleted uranium chips (Dow Chemical, 1971) and plutonium chips
coated with lathe coolant. The drums are still present in this trench.
.:
3.
OU Sum Pit No.2 Site OHSS Ref. No. 153) - OU Sum Pit No.2 is actually two parallel trenches which
were used in 1957 and from 1961 to 1965 to bum 1,082 drums of oil containing uranium (Rockwell
International. 1987b). The residues from the buming operations and some flattened drums were
covered with backfill. Clean-up operations were performed in the 1970s (Rockwell International, 1987b).
.
4.
Pallet Sum Site (IHSS Ref. No. 154) - An area southwest of on .Sum Pit No.2 was reportedly used to
destroy wooden pallets in 1965. The types of hazardous substances or radionuclldes that may have
bee"n spilled on these pallets is unknown. Clean-up actions were performed in the 1970s (DOE, 1986).
2.1.2.3 East Trenches Area
The East Trenches Area consists of nine burial trenches and two spray irrigation areas (Figure 2-2).
The trench numbers and their respective IHSS designations are:
Trench T -3 - IHSS Ref. No. 110
Trench T -4 - IHSS Ref. No. 111.1
Trench T -5 - IHSS Ref. No. 111.2
Trench T ~ - IHSS Ref. No. 111.3
Trench T-7 -IHSS Ref. No. 111.4
Trench T -8 - IHSS Ref. No. 111.5
Trench T -9 - IHSS Ref. No. 111.6
Trench T-10 -IHSS Ref. No. 111.7
Trench T -11 - IHSS Ref. No. 111.8
Trenches T -3. T-4, T-10. and T-11 are located north of the east access road. and trenches T-5 through
T -9 are located south of the east access road. The trenches were used from 1954 to 1968 for disposal of
depleted uranium. flattened depleted uranium and plutonium-contaminated drums, and sanitary sewage sludge.
The wastes have not been disturbed since their burial.
SURFACE WATER INTERIM REloIeow. AC'T1ON PI.AN
~I(V ......r5 "'"ANT. GOI..DEN. CO'..ORACO
eg&; ......rac'..,.,,.,\Jt~MC.2.mar
JwfIarcr '99'
-------
IHSS numbers 216.2 and 216.3 are part of the East Trenches Area and are designated as IHSSs
"
because they were used for spray irrigation of sewage treatment plant effluent. The historical discharge of
Pond B-3 was to this spray irrigation area. This practice has been terminated however, and the current Pond
B-3 discharge is sent to Pond B-4.
.
2.1.3 Surroundina Land Use and PODuiation Densitv
The RFP is located in a rural area (Figure 2-3). Approximately 50 percent of the area within ten miles
of the RFP is in Jeffersan County. The remainder is located in Boulder County (40 percent) and Adams
County (10 percent). According to the 1973 Colorado Land Use Map, 75 percent of this land was unused or
was used for agriculture. Since that time, portions of this land have been converted to housing, with several
new housing subdivisions being started within a few mUes of the buffer zone, southeast of the plant site.
A demographic study, using 1990 census data, shows that approximately 1.9 million people lived within
the eight-county Denver metropolitan region. This region covers approximately 5.076 square miles and
includes the following counties: Adams. Arapahoe. Boulder, Denver, Douglas, Jefferson, Clear Creek, and
Gnpin. The most populated sector Is to the southeast, toward the center of Denver. This sector had a 1989
population of approximately 600,000 people living between 10 and 50 miles from Rocky Flats. Recent
population estimates registered by the Denver Regional Council of Governments (DR COG) for the eight-county
Denver metro region have shown distinct patterns of growth between the first and second halves of the
decade. Between 1980 and 1985. the population of the eight-county region increased by 197,890. a 2.4
percent annual growth rate (DRCOG, 1989). Between 1985 and 1990 a POPulation gain of 80.875 was
recorded, representing a 0.9 percent annual increase. The 1990 population showed an increase of 9.300 (or
0.5 percent) from the same date In 1989 (DRCOG. 1990).
The RFP is approximately located in the center of RFP legal land area which is approximately 3 miles
(north-south) by 4 miles (east-west). There are eight public schools within six miles of the RFP. The nearest
SURFA.CE WATiOR IN'TCRIIooI REMEDIAL A.CTION PI.AN
ROCI(\' ~l.ATS P\.»lT. GOI.DEN. CO\.OAAOO
89&. --._"\Jt'_.2.mar
MarcF'l '99'
-------
~
I
-N-
a
EXPLANATION
t2 Industrial/Business
...-,
LJ
~ Urban Residential
Q Suburban Residential
I I I
o 2 .3
miles
Boulder
"'::':~:~~S:~:\::\~:.:..,
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.;:::::::}
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..
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Springs ". ,','
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N
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(after: .Jefferson County Planning and Zoning Deportment. April, 1990)
en
o
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FIGURE 2-3
LAND USE IN THE VICINITY OF ROCKY FLATS
P LA NT
SURFACE w...~ ~- REIIIECIAL ACTION ""-""
ROCX'!' ~.....'!'s ~. GOU)EN, CO\.ORAOO
0;&&'.-.- _n",._.z'.....
MatCrI 199'
-------
educational facUlty Is the WItt Elementary School, which is approximately 2.7 miles east of the Plant buffer zone.
The closest hospital Is Centennial Peaks Hospital, located approximately seven miles northeast. The closest
...
park and recreational area Is the Standley Lake area. which is approximately fIVe miles southeast of the Plant.
Boating, picnicking, and limited overnight camping are permitted. Several other small parks exist in
..
communities within ten mUes. The closest major park, Golden Gate Canyon State Park, located approximately
15 miles to the southwest, provides 8,400 acres of general camping and outdoor recreation. Other national
and state parks are located in the mountains west of the RFP. but all are more than 15 mles away.
Some of the land adjacent to the Plant is zoned for industrial development. Industrial facilities within
five mUes include the former TaSCa (The 01 Shale Company) laboratory (40-acre site located two mUes south
and now occupied by Analytica, Inc.), the Great Western Inorganics Plant (two mUes south), the Frontier Forest
Products yard (two mUes south), the Idealite Ughtweight Aggregate Plant (2.4 mUes northwest). and the
Jefferson County Airport and Industrial Park (99O-acre site located 4.8 mUes northeast).
Several ranches are located within ten mUes of the Plant, primarily in Jefferson and Boulder Counties.
They are operated to produce crops, raise beef cattle, supply mAk. and breed and train horses. According to
the 1987 Colorado Agricuttural Statistics, 20,758 acres of crops were planted in Jefferson County (total land
area of approximately 475,000 acres), and 68,760 acres of crops were planted in Boulder County (total land
area of 405,760 acres). Crops consisted of: winter wheat, com. baney, dry beans, sugar beets, hay. and oats.
livestock consisted of: 5,314 head of cattle, 113 hogs. and 346 sheep in Jefferson County, and 19,578 head
of cattle. 2,216 hogs, and 12,133 sheep In Boulder County (Post, 1989).
2.2
AFFECTED AND SENSmve ENVIRONMENT
2.2.1
Phvsical Environment
The natural environment of the Plant and vicinity is influenced primarily by Its proximity to the Front
Range of the Rocky Mountains. The Plant is directly east of the north-south trending Rocky Mountains, with
SURF ACE WATER INTeRIM FlEMEOIAL ACTION PlAN
ROCI(V ~I.A TS PI.ANT. GOlDEN. COLOAAOO
89&; _._'-"ut'-.2."""
Marcn ~ 99'
-------
an elevation of approximately 6,000 feet above sea level. The RFP is located on a broad. eastward-sloping
plain of overtapping alluvial fans developed along the Front Range. The fans extend about fIVe miles in an
..
eastward direction from their origin in the abruptly rising Front Range and terminate on the east at a break in
slope to low roiling hDls. The continental divide Is about 16 mUes west of the Plant. The operational area at
the Plant is located near the eastem edge of the fans on a terrace between stream-cut valleys (North Walnut
.
Creek and Woman Creek). The Rocky Fiats Alluvium (the deposit of coalescing alluvial fans) Is exposed at the
surface and consists of a topsoil layer undertain by as much as 100 feet of silt. clay, sand. and gravel.
The RFP Is situated In a semiarid region that averages 15 inches of annual precipitation. Forty percent
of the yearty total comes in the spring, much of It in the form of snow. Of the balance. 30 percent is accounted
for by summer thunderstorms, with the rest occurring in the fall (11 percent) and winter months (19 percent).
Average yearty snowfall is 85 inches. Runoff control structures exist to channel surface water from the Plant
to monitoring ponds. These structures are sized to accommodate the 100-year storm event which is equivalent
to four inches of rain in a six-hour period.
Mineral resources found In the vicinity of RFP include sand, gravel. crushed rock. clay, coal. and
uranium. There are no known clay, coal or uranium deposits within the RFP buffer zone; however. these
commodities are mined in the region, within 20 mDes of the plant. The Schwartzwaider Uranium Mine is
located approximately four mDes southwest of the RFP. The mine has been the largest producer of vein type
uranium ore In Colorado and ranks among the six largest of this type In the United States (DOE. 1980). Active
sand and gravel mines lie within the buffer zone boundaries. There Is an aggregate processing facility adjacent
to the northwest comer of the buffer zone which reopened in 1989. 00 and natural gas production is also
active in nearby northwest Adams County and east central Boulder County.
Oil and natural gas activity near Rocky Fiats Plant includes oilfield developments. pipeline. and
production operations. The closest major oil and gas fields are in northwest Adams County (Jackpot and
Spindle Fields), and a smaller field occurs in east central Boulder County (Boulder Field). A natural gas
pipeline that originates in Wyoming and proceeds across eastem Colorado into Oklahoma is located
SURFACE W"'!EFlINTERI'" REMEDIAL "C'T1ON PlAN
R:)O(V ~V.TS "UINT, GOU>EN, COlOAADO
.;"--,_"",\_.2.",,,
Martl"l ~99'
-------
approximately ten mUes north of the Plant in southern Boulder County. Local natural gas pipelines cross the
south side of the Rocky Flats Plant. The nearest refinery operation is the Conoco Refinery located in
...
Commerce City about 20 mUes east of the Plant. A north-south oriented oil pipeline feeds in to the refinery
from fields in northeastern Colorado and southeastern Wyoming (Donaldson and MacMillan, 1980).
.
There are four main drainages from the Plant property as shown on Figure 2~. North Walnut. South
Walnut, Rock and Woman Creeks all have intermittent streams which provide drinking water and irrigation
water. T~ere are a number of ditches crossing the area as well. conveying water collected off site to other
areas, the Plant, Walnut Creek, or Woman Creek. UntO late 1974, Plant wastewater had been discharged to
Walnut Creek, and untU 1975, filter backwash from the raw water treatment plant went into Woman Creek.
All process wastewater is now either recycled or disposed through evaporation. Sanitary wastewater is
discharged In accordance with the RFP's NPDES permit effluent requirements.
2.2.2 Reaional and Local Hvdroaeoloav
The stratigraphic section that pertains to the RFP includes. in descending order, unconsolidated surficial
units (Rocky Flats Alluvium, various terrace alluviums, valley fill allUvium, and colluvium) (Figure 2-5), Arapahoe
Formation, laramie Formation, and Fox Hills Sandstone (Figure 2~). Ground water occurs under unconfined
conditions In both the surficial and shallow bedrock units. In addition, confined ground-water flow occurs in
deeper bedrock sandstones.
2.2.2.1 Alluvial Materials
The Rocky Flats Alluvium underlies a large portion of the Plant. The alluvium is a broad planar deposit
consisting of a topsoU layer underlain by up to 100 feet of peony stratified silt. clay. sand, gravel and cobbles.
Unconfined ground-water flow occurs in the Rocky Flats Alluvium which is relatively permeable. Recharge to
the alluvium is from precipitation, snowmelt, and water losses from ditches, streams. and ponds that are cut
into the alluvium. General water movement in the Rocky Flats Alluvium is from west to east and toward the
$URFAICE WAITE'" 1NT'E""to,I ~to,IEOIAl ACT10N PI.AN
~I(Y .'-":$ P>,JINT. GOLDE'-. COlOfWXl
¥i"-''8I>._nUl,_'2.mat
Marc:n 1991
-------
v"."'--- ------- ./
{ / ~}
----
(
\
/ Y./E-. /
..,/ /--1' /\ -,Y
\ "". / /j / (
80ulder Co
--- - oJ,Har,on c.o
Color.do 128
J
~
/
/
-.;;: . Odell \
8~ --- ".~ ~ -~. ---- -.J'
~~..~ / \! '~=---.""" .~ .
..........~~ .. -=- ~ \;
~ . '--- 1
----- ~ '\.. \ ~ '\ \" ,,"-, (j) V
~Y:~ I . ~ 1~~~~ ~~)'~.
~ ~ I . r-"'!.-.WtJlnu' .v-". ---.!"\.-.
<:) ~ '\.S.~G - "--- .J
~
'\
.. ~ -. --- .--< r - ~ --./...
"'--... ~ ~ " ~ ~ '- -----
~ ~ I .~ ~ I ~; f=~ '
~ "----.~ ." /':~?~~- ;/\
~. ' C_~~I--\ "
,,---) ""
~ L..f'--- ~
" ...,
~ ~.
- ~ (
\
.---'"
e... Ace... Aoad
~~
" ~
\~ \
~.
~ .-0-
/ ....
IIp~. :'.,:
T.,. .0" ~... /\...
. ...~.
1.._-~: 1.lJ".,
: ------- . . ;",If LOk. ~
_.. ---'
~ ----. --..--..-
~ ~ '---- ---z.
~
~Z~NE- -
'"
--\
- t (after. Roc'w" "t...at""~ 19860,
~ U.S.G.S. Quad.., Louisville, 1979,
Golden, 1980, and Lafayette, 1979)
o 112 1 m'"
~~
:-=-.. ~.
~.
~ ?
Js
(~ /'
FIGURE 2-4
SURFACE WATER
DRAINAGE PATTERNS AT
-------
./ .../' ~,--- ----- J'" - ..-, "
'" /' ""."on Co
/; / //'~~
, /' -r" / / / ~,-L
/" /J ,/ ' ..------ ------ ~
i t' / /:./ / u.s, DEPAIITME.:oF EMERGT - ~
\! / / // /-- ~ ..- ~y'
\ ,1/:/ / ""'-.~../ /
,/" .,~~ ~-----
t,p ;:7 ";~~'" ".._~.
\ I Rocky Flata P
Woo, Ace... A... lent
SOU'h
~-;;--I.Y"'-.~~~
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. 7
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RJJ014A.PJ-080190
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WEST
800
o
ROCKY RATS PLANT SI1E
Colluvium
Verda. Alluvium
"""'.."""'''''':.'''-''.''''''''''''''':':.'''','''.-,
--
MODERN STR~OO ~ - - -
XlM41£Ly 20 A:Er PER ~ -
'"
,
fAST
T erroce Alluvium
Volley Fill
1.
)
---
NOT TO SCAlE
(after. Scott, 1960)
FIGURE 2-5
EROSIONAL SURFACES AND ALLUVIAL DEPOSITS
-------
-
...
AGE FORNA110N
I ~ Gnten
I Nountoin
~ Denver
Arapahoe
Laramie
Fox Hills
:0'0. ..., . '0."
. .00...0..,
8 ~. .' ...'. . . '0 .
CQ :Ck':~'O'.:Q' .
.\)..' .". '0
o -- - Yellowi8lt-brown to gr:ayiItt oev. fluvial tuffac8ou8 ~. siIt8tane. and
~ .... ..,:., ~~. eandItone b~ WIth CCIft9Jotn8rat. and ~ray mudflon
YtllowiIh-9rGy to YtUowIItt-brown 8CIndItDI.e;' 8IItItone: and clay8tone;
di8contlnuoua ~ at bale
~. 1Ine-to-1TIIdIurn~ 8ClndltDl1I and 8IIty clayI; thin cool btd8 in
loW part
GRAPHICS
SUMMARY DESCRIPTION
t
i '.:.:,:.:-:.:.:.:.:-:.:.:.:.:: - Tan,fine-t.o-fntdium-9ra _~II and 1CIIIdy'" ,
..
en
;:)
0
~ Pierre
t:J
a::
(,) ...
IS
a..
a..
;:)
Niobrara
Benton
DcI'tt Pt. 8IIty tIIOIt and f.. ttIIn. 8IIty ~
- DcI'tt FfIf. ywy caIccnou8 8IIaII. 8ForaminIf..o abundant (Smoity Hi1Ia Memlllr) I
".""""." ..'. . Ught 9rGy. ..... ~ IImIItDnt (Fort HayI WImbIr) I
""- Brwn. tandy. foIIIIIftrol8 IImtItant
DcI'tt fJffI1 8haII with bIntDnft8 ItrIaIc8; thin IIrnt1tDn81 In middle part; f.. I
~~ concntionI in Iowr part
DcI'tt FfIf. brittle IIIty ... (WowTy) .
as ~ I So. Platte
~_i- j L~
~
I
e
:;,
~
t-
1(,)
~~
j
:E
f5
_c:.-
j
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z:
z:
LoJ
a..
i
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~
i
I
i
Morri8on
Rallton Cr8ek
Lykina
Lyon8
Fountain
~ ~~ locally congIomtratk IGIIdItone; frwquent
~ :=~::::::~~: - = ~ ~ = ::: ~tIIln IIrnt8tDMt In mlddlt
IJ9I.It tan IIIt:ItDnt and IgIIt reel; 8IIty IIIaIt; ~ 1CIfIOIII:)c.. at bale
arid locally COIIg\am8'atk
Red IIItItane with two IaminatId ~ In lower part
Qrayilft-wllfta. ~tD-meclum-traln8d cn8-btcIdtd ICIIIdItone;
~"(ltL -- frwquW
:':':-:'::::" .:- Red. ~Intd IGIIdItDIII and ~ artUIIic; ttdn,
: : . : : : ~. ltnticuIar rwd 8IItItDn8i frwquent thrauput
PRECAMBRIAN
(modIfitd from: LeRoy and Wtimer. 1571)
..
+ + CntIII. ICIIIIt. and amaU vnmJtic intNIIanI
+
FIGURE 2-6
GENERALIZED STRATIGRAPHIC SECTION
SURFACE WA~ IHTEA/oI REMEDIAL ACTION ~
AC:XXv F\.ATS !>\.ANT. GOI.DEN. CO!..ORAOO
89&9' -,- '-"111'._.2."'"
Marc'"" '99'
-------
drainages. Ground-water flow is also controlled by sediment drainages in the top of bedrock. The water table
in the Rocky Flats Alluvium rises in response to recharge during the spring and declines during the remainder
\.
of the year. Discharge from the alluvium occurs at minor seeps in the colluvium that covers the contact
between the alluvium and bedrock along the edges of the valleys. au 2 Is situated on a terrace of Rocky Flats
,.
Alluvium that thins east of the Plant and does not directly supply water tQ wells located downgradient of Rocky
Flats.
Various other alluvial deposits occur topographically below the Rocky Flats Alluvium In the Plant
drainages. Colluvium (slope wash) mantles the valley side slopes between the Rocky Flats Alluvium and the.
valley bottoms. In addition, remnants of younger terrace deposits including the Verdes. Slocum. and Louviers
Alluvia occur occasionally along the valley side slopes. Recent valley fill alluvium occurs in the active stream
channels.
Unconfined ground-waterflow occurs in these surficial units. Recharge is from precipitation, percolation
from streams and ditches during periods of surface water runoff, and by seeps discharging from the Rocky
Flats Alluvium. Discharge is by evapotranspiration and by seepage into other geologic formations and streams.
The direction of ground-water flow is generally downslope through colluvial materials and then along the course
of the stream in valley fill materials. During periods of high surface water flow, water is lost to bank storage
in the valley fill alluvium and returns to the stream after the runoff subsides.
2.2.2.2 Bedrock Matertiils
The Cretaceous Arapahoe Formation underlies surficial materials beneath the Plant. This formation is
a fluvial deposit composed of overbank and channel deposits. It consists primarily of claystone with some
sandstone and is near1y flat lying beneath the Plant Oess than a two-degree dip) based on the draft seismic
profiling report (Rockwell International. 19898). The sand bodies within the claystone are composed of fine-
grained sands and silts, and their hydraulic conductivity is relatively low compared to the over1ying Rocky Flats
SURFACE WATER IPr.ERlIooI FlEIooIEOIAI. ACTION F'l.AN
ROCI
-------
Alluvium. A high resolution seismic reflection survey is ongoing at the Plant to further characterize bedrock
geology.
J
The Arapahoe Formation is recharged by ground-water movements from overiying surficial deposits
and by leakage from streams. The main recharge areas are under the Rocky Aats Alluvium, although some
.
recharge from the colluvium and valley fill alluvium likely occurs along the stream valleys. Recharge is greatest
during the spring and ear1y summer when rainfall and stream flow are at a maximum and water levels In the
Rocky Flats Alluvium are high. Ground-water movement in the Arapahoe Formation Is generally toward the
east, although flow within Individual sandstones Is not fully characterized at this time. Regionally, ground-water
flow In the Arapahoe Formation is toward the South Platte River in the center of the Denver Basin (Robson,
1981a).
The Laramie formation under1ies the Arapahoe and is composed of two units, a thick upper claystone
and a lower sandstone. The claystone is greater than 700 feet thick and Is of very low hydraulic conductivity;
therefore, the U.S. Geologic Survey (Hurr, 1976) concludes that Plant operations WIll not impact any units
below the upper claystone unit of the Laramie Formation.
The lower sandstone unit of the Laramie Formation and the under1ying Fox Hills Sandstone comprise
a regionally important aquifer in the Denver Basin known as the Laramie-Fox Hills Aquifer. Aquifer thickness
ranges from 200 to 300 feet near the center of the basin. These units subcrop west of the Plant and can be
seen In clay Pits excavated through the Rocky Flats Alluvium. The steeply dipping beds of these units west
of the Plant (a~mately a SO-degree dip) qulcldy flatten to the east ~ess than two-degree dip) based on
preliminary resutts of the high resolution seismic reflection study (Rockwellintemational, 1989a). Recharge
to the aquifer occurs along the rather limited outcrop area exposed to surface water flow and leakage along
the Front Range (Robson, 1981b).
Sixteen wells were completed in various zones within bedrock during the 1987 drilling program at au 2.
Although claystone was the most frequently encountered lithology immediately below the alluvium/bedrock
SURFACE WATER INTERIM REMEDW. AC'T1ON P\.AN
ROCX\' ~LATS PI.ANT. GOI.!)EN. COlORAOO
8;&.;I-_I_n,,"_-2.......
Marc~ '99'
-------
contact. interbedded sandy, silty and lignitic units with both gradational and sharp contacts were present as
s.
well. All of the bedrock encountered directly beneath surficial materials was weathered. and some saturated
sandstones were encountered.
J
2.2.3 Site Hvdroloav
2.2.3.1 Surface Water
Surface water drainage patterns at the RFP are shown on Figures 2-2 and 2-4. A discussion of the
major au 2 surface water features. including the South Walnut Creek and Woman Creek drainages, is
presented below. Although this 1M/IRA Plan addresses collection and treatment of contaminated South Walnut
Creek Basin surface water; the Woman Creek drainage is included in the following discussion to provide a
complete description of au 2 hydrology. Collection and treatment of Woman Creek Basin seepage southeast
of the 903 Pad Area wUl be addressed In a separate 1M/IRA Plan as discussed in Section 1.
South Walnut Creek
The headwaters area of South Walnut Creek has been filled during construction of RFP facilities. As
a result. flow originates from a buried culvert located west of Building 991. Flow in the upper reach of South
Walnut Creek Is directed to the south d Building 991 and under the Perimeter Security Zone (PSZ) fence by
a buried met8J corrugated cUv8rt. The culvert outlet Is located in the South Walnut. Creek drainage
approximately 500 feet downgradlent of the PSZ fence near the discharge of the sewage treatment plant (see
Figure 4-2). A concrete cutvert and a second metal corrugated culvert also discharge into the South Walnut
Creek drainage just downgradient of the PSZ fence and north of the Mound Area. The flow from the concrete
culvert originates as seepage from the hOlside south of Building 991 and flows into a ditch along the slope.
The metal corrugated culvert drains plant runoff collecting in a drainage south of the PSz. The combined flow
then enters the South Walnut Creek detention pond system. Below the detention ponds, South Walnut Creek,
North Walnut Creek, and an unnamed tributary join within the buffer zone to form Walnut Creek. Great Western
SURFACE WATER INTERIM REMEDIAL. AC'T1ON PlAN
qoocy FLATS PI.ANT. GOI.DEJoj. COLOI\AOO
89&;\ """1f8C\~ut \MC.2.m&r
Marcl'l ~99'
-------
Reservoir is located approximately one mile east of this confluence and is a drinking water source for
Broomfield. Flow is routed around Great Westem Reservoir by the Broomfield diversion canal.
.~
The South Walnut Creek detention pond system consists of five ponds (B-1, B-2. B-3. B-4, and B-5) that
retain surface water runoff and RFP discharges for flood control. and for monitoring and treatment prior to
"
downstream release. All flow in the pond system is eventually detained in Pond B-5, where it is treated and
monitored prior to discharge. Water is discharged from Pond B-5 in accordance with the Plant's NPDES permit
(discharge point 006). Ponds B-1 and B-2 are reserved for spUi control, surface water runoff, or treated
sanitary waste of questionable quality. Pond B-3 is used as a holding pond for sanitary sewage treatment plant
effluent. The historical discharge of Pond B-3 was a spray irrigation system located in the vicinity of the East
Trenches. This practice has been terminated, however, and the current Pond B-3 discharge is sent to Pond
B-4. In addition to Pond B-3 discharge, Ponds B-4 and B-5 receive surface water runoff from the central
portion of the Plant. The surface water runoff received by Pond B-4 is collected by the Central Avenue Ditch
and the South Walnut Creek Drainage.
Woman Creek
Woman Creek Is located south of the Plant, with headwaters in largely undisturbed Rocky Flats
Alluvium. Runoff from the southern part of the Plant is collected in the South Interceptor Ditch located north
of the creek and delivered downstream to Pond 0.2 (see Figure 2-2). Pond C-1 (upstream of 0.2) receives
stream flow from Woman Creek. Flow In Woman Creek is also influenced by diversion 01 water from Rocky
Rats Lake Into the creek by local landowners. The discharge from Pond 0.1 is diverted around Pond C-2 into
the Woman Creek channel downstream. Water in Pond 0.2 is treated and monitored prior to discharge.
Discharge from Pond 0.2 is In accordance with the Plant's NPDES permit (discharge point 007). Historically,
discharge from Pond 0.2 has been to Woman Creek, however, since October of 1989. treated water is being
pumped to the South Walnut Creek drainage and flows off site via the Broomfield diversion canal.
SURFACE WA~" IN'TERIIoI REloIeow. ACTION PI.AN
ROCXY .i.ATS P\.ANT. GO(.OEN. CO\.ORAOO
eg&Q\-_\~Ut\_.2.11\8t
Marc" 19&1
-------
Flow in Woman Creek and the South Interceptor Ditch is intermittent. This has been observed by field
investigation crews since 1986 and is indicative of frequent interaction with the shallow ground-water system.
\.
4
2.2.3.2 Ground Water
Ground water occurs in surficial materials (Rocky Flats Alluvium, colluvium, and valley fill alluvium) and
in Arapahoe sandstones and claystones at OU 2. These two flow systems. which are hydraulically connected
at shallower portions of the Arapahoe Formation, are discussed separately below.
Ground Water in Surficial Materials
Ground water is present In the Rocky Flats Alluvium, colluvium, and valley fill alluvium under unconfined
conditions. Recharge to the water table occurs as infiltration of incident precipitation and as seepage from
ditches and creeks. In addition, detention ponds along South Walnut Creek and Woman Creek recharge the
valley fli alluvium. Figure 2-7 shows the potentiometric surface of uppermost ground water measured between
April 4 and April 8, 1988, and the locations of alluvial and bedrock wells in the vicinity of OU 2.
The shallow ground-water flow system is quite dynamic, with large water level changes occurring in
response to precipitation events and stream and ditch flow. For example, between mid-April and September,
1986, water leVels In wells 1-86 and 4-86 (completed in valley fill alluvium) dropped more than four and eight
feet, respectively. Alluvial water levels are highest during the months of May and June. Water levels decline
during late summer and fall, and some wells go completely dry at this time of year. Ground-water flow in the
Rocky Flats Alluvium is generally from west to east, following the surface of the claystone bedrock.
Alluvial ground water discharges to seeps, springs. surface water drainages, and subcropping Arapahoe
Sandstone at OU 2. Seeps and springs occur along the edge of the Rocky Flats Alluvium terrace (at the
alluvium/bedrock contact) and on the side slopes of the terrace. Seeps and springs on the terrace side slopes
SURFACE WATER INTERIM FIE/ooIEOW. ACTION PLAN
ROCI(V F\.ATS~. GOLOEN. COLOIWX>
011&.; I__,_n.., 1 _.2.....,
Marc'" '99'
-------
EXPLANATION
.
c:J
INI)IVI)t.W. IWMDOUS SUBSl'ANCE
SITE (ftiSS)
~ ...
...
r~/\.
/ ;.---- \
~~," ~
/I~- ~ \ )
- / 3986 I
. ~. "/" ~---_.-' \ 6880 i
~~//. I / j U I
..J/---' / / / I
-. /) / /
~ / 'Jca'/,r/ / / 7'/)
.,-:--/ ~: .~/ 7.£""-:~" "."~
~-_.__// '- .~~~. ,rjJ~ .' / - - '. '
/' /~ ,..., ~\) /
- - -' <-:J~' \)
. ~' /.... ~~~ ;'
" -;- --~/:;/ ~ /_'J~~~/
/') ( --- --- ~ /'J,\~Q
~ -j r~- i7,!--/
~.~/...:
POND H
6798
P01'EHT1OWETRIC SURfACE
ElIVATION (fMt abcM
mean I8G 1M)
)S86
All. D,\TA BASED ON WEASUREYOO'S
YADE APRIl. 4-8. 1988 INCt..IJSM
UNE OF EQUAL POmlT1OWE1RIC
'--586'" SURfACE ElIVA110N (fMt
"" abcM mean I8G 1IwI}-OASHED
WI£RE APPROXDoIATElY LDCAlED
ND
NO D,\TA
2587 . BEDROCK WONrT'OR WEll
3789 0 AI.1.IJVW.. WONITOR WEll.
0382 Ii. PRE-1988 WONITOR WEll
~
a
Scale: 18 = 600'
0'
I
JOO'
I
600'
I
CONI'OUR 1HItRVAl. - 20'
~" ".---
" .._-~- ",/
U.S. DEPARTMENT OF ENERGY
Rocky Flats Plant
Golden, Colorado
'. ~.
=
-.-
OPERABLE UNIT NO.2
SURFACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
FIGURE 2-7
POTENTIOMETRIC SURFACE OF THE
UNCONFINED GROUND-WATER
FLOW SYSTEM
:-2
. -
-
. .
~.
'.
:/
...,..
...,.,..
'..
March. 1991
-------
...
'"
'"-"". '.~' -- - .-:..".
,
~ ---
-
. .
08786
,oj..
,
/.
,
.'.
t
.~;. .'
. .-
.... '.... -. -. - ~..:. .
"
'/
-I ~~
. ,
...
-:-
---::- '. -'
. .
,.~
'. .,:!"
-
~
i
"
~
iii
i
. '-.;
.__:..:..;
__A -'.
-
~7'-'-~-::;-
. :---:---
~ .;
.----
'.
POND C-2
. . -
-
-
.', ..~~-:.:...:::...~-
-..:.~ .
-..
-------
may be due to thinning of colluvial materials. Ground water in colluvial materials south of the 903 Pad and
East Trenches Areas discharges to the South Interceptor Ditch, and ground water in valley fill materials
~,
discharges to Woman or South Walnut Creeks.
411
Hydraulic conductivity values were estimated for surficial materials from drawdown-recovery tests
performed on 1986 wells during the initial site characterization and from slug tests performed on selected 1986
and 1987 wells during the Phase I RI (Rockwell I ntemational , 1987a). The average ground-water velocities in
the Rock)L Flats Alluvium, Woman Creek Valley FUI Alluvium, and South Walnut Creek Valley FUI Alluvium are
84 ft/yr, 145 ft/yr, and 20 ft/yr, respectively (Rockwell I ntemational , 1987a). These values are based on a
horizontal gradient of 0.02 feet/feet (ft/ft), an effective porosity of 0.1, and mean hydraulic conductivities of 4 x
10", 7 x 10" and 9.5 x 1006 cm/s for Rocky Flats, Woman Creek Valley FBI and South Walnut Creek Valley Fill
Alluvium. respectively. The calculations assume year-round saturation. However, as discussed above, portions
of the Rocky Flats Alluvium, colluvium, and valley fill alluvium are not continuously saturated. Thus, the shallow
ground water must flow at less than the calculated annual average velocities. The reactivity of dissolved
constituents could further reduce contaminant migration rates below estimated ground-water velocities.
Bedrock Ground Water
The greatest potential for ground-water flow in the Arapahoe Formation occurs in the meandering
lenticular sandstones contained within the claystones (Le., the basal formation) due to their relatively higher
permeability. Flow within individual sandstones is assumed to be from west to east, but the geometry of the
bedrock ground-water flow path is not fully understood at this time due to its dependence upon the continuity
of the sandstones and their hydraulic interconnection (Robson, 1981 a). Ground-water recharged to sandstones
occurs as infiltration from alluvial ground water where sandstones sUbcrop beneath the alluvium and by leakage
from claystones overlying the sandstones. Ground-water from the basal formation of the Arapahoe aquifer is
used for irrigation, livestock, watering, and domestic purposes. Wells are located east of the RFP within the
Denver Basin.
SURFACE WATER IIoITERIM REMEDIAl. ACTION P\.AN
ROO(V "LATS PlANT. GOI.OEN. CO!.OIW)O
89109'.-'-'-"""._.2,,,,,",
Marc:'" '9S'
-------
There is a strong downward gradient between ground water in surficial materials and bedrock. Vertical
gradients range from 0.31 ft/ft between wells 35-86 and 34-86 to 1.05 ft/ft between wells 41-86 and 40-86.
j
These gradients imply a relatively high hydraulic conductivity contrast between the surficial materials and
bedrock, which is supported by hydraulic conductivity test results.
.
Flow within sandstones is regionally west to east. The geometry of the ground-water flow path in the
bedrock is not fully understood at this time because it depends upon the continuity of the sandstones and their
interconn~ion. Evaluation of the lateral extent and degree of interconnection of the sandstone units is a
primary goal of the Phase II and Phase III Remedial Investigations for OU 2.
Hydraulic conductivity values for Arapahoe sandstones were estimated from drawdown-recovery tests
performed In 1986. slug tests performed in 1987, and packer tests performed In 1986 and 1987. The maximum
horizontal ground-water flow velocity in sandstone is 75 ft/yr using a hydraulic conductivity of 83 ftjyr, a
horizontal gradient of 0.09 ft/ft. and an assumed effective porosity of 0.1.
2.2.4 Ecoioav
Within the Plant boundaries a variety of vegetation thrives. Included are species of flora representative
of tall grass prairie. short grass plains. lower montane. and foothill ravine regions, with none being on the
endangered species list. It is evident that the vegetative cover afong the Front Range of the Rocky Mountains
has been radically altered by human activities such as burning, timber cutting. road building, and overgrazing
for many years. Since the acquisition of the RFP property, vegetative recovery has occurred as evidenced by
the presence of grasses like big bfuestem and sideoats grama (two disturbance-sensitive species). No
vegetative stresses attributabfe to hazardous waste contamination have been identified (DOE, 1980).
The animal life inhabiting the RFP and its buffer zone consists of species associated with western prairie
regions. The most common large mammal is the mule deer, with an estimated 100 to 125 permanent
residents. There are a number of small carnivores. such as the coyote, red fox. striped skunk, and long-tailed
SURFACE WATE'lIIo/TERlM RE"'Eow. ACTION PI.AN
ROCKV ~L.4 TS P\.ANT. GOlDEN. COI.ORACO
eg&g'-- ,...nUl ,_.2."'"
U.rc~ '9&'
-------
weasel. A profusion of small herbivore species can be found throughout the Plant and buffer zone consisting
"
of species such as the pocket gopher, white-taRed jackrabbit, and the meadow vole (DOE. 1980).
Commonly observed birds Include western meadowtarks. horned larks, mourning doves. and vesper
.
sparrow. A variety of ducks. killdeer, and red-winged blackbirds are seen In areas adjacent to ponds. Mallards
and other ducks frequently nest and raise young on several of the ponds. Common birds of prey in the area
include marsh hawks, red-tailed hawks. ferruginous hawks. rough-legged hawks. and great horned owls (DOE.
1980). .
Bull snakes and rattlesnakes are the most frequently observed reptDes. Eastern yellow-bellied racers
have also been seen. The eastern short-homed lizard has been reported on the site. but these and other
lizards are not commonly observed. The western painted turtle and the western plains garter snake are found
in and around many of the ponds (DOE. 1980).
2.2.5
Sensitive Environments and Endanaered SDeCies
The Endangered Species Act of 1913 (Public Law 93~205). as amended. provides that all federal
agencies implement programs for the conservation of listed endangered and threatened species. Federal
agencies must ensure that actions authorized, funded. or carried out by them will not jeopardize the continued
existence of any endangered or threatened species.
The U. S. Fish and WIldlife Service (USFWS) has indicated that the two endangered species of interest
in the RFP area are the bald eagle and the black-footed ferret (Rockwellintemational. 1988c). Prairie dog
towns provide the food source and habitat for ferrets. Since there are no prairie dog towns in or near the 881
Hillside Area which Is near the 903 Pad. Mound and East Trenches, the USFWS has determined that ferrets
probably do not exist in the investigation area. Bald eagles are occasional visitors to the area. primarily during
migration times. Sightings are rare and little suitable habitat exists on the RFP site other than some perching
locations. No nests are found on the RFP site. The proposed action will not adversely affect the bald eagle.
SURFAce WA~ INTERIIoI REIoIECIAL AC'T1ON PI.AN
ROCI(V FL.}.TS FV.>(T. GO\.DE". COlOAAOO
ega.;'_''''''._nUl'._-2.mar
Uarcl"l 199~
-------
The USFWS has concurred with these findings subsequent to a field visit on 15 June 1988 (Rockwell
International, 1988c).
J
Other animal species of interest that exist in the RFP area include burrowing owls and Swainson's
hawks. Cottonwood trees within approximately one quarter mile of the 903 Pad, Mound, and East Trenches
6.
Areas were investigated to determine if any raptor nests exist and none were found. The nearest population
of burrowing owls Is approximately two miles to the east. The nearest population of Swalnson's Hawks could
be in the cottonwood trees in the area of the North Walnut Creek or Rock Creek drainages, north of the 88 1
HUiside area.
The 903 Pad, Mound, and East Trenches Areas are not used, nor intended for use, as a public or
recreational area. nor for the development of any unique natural resource. No unique ecosystems were found
at the RFP during extensive biological studies (DOE, 1980).
2.2.6 Wettands
Initial consultation with the USFWS and the U.S. Army Corps of Engineers was conducted in the spring
of 1988. Wetlands at the RFP site were delineated. The proposed action is not located in the delineated
wetlands. Aerial photography imagery for the 903 Pad. Mound, and East Trenches Areas was examined for
wetlands identification followed by limited site inspection (EG&G, 1990b). Two isolated stands of wetlands
vegetation containing common cat-taU ~ latifolia) were located primarily within IHSS 140, where ground
water flowing toward the terrace edges emerges as seeps or springs at the contact between the alluvium and
bedrock. The two areas are each less than 20 square feet In size.
Unear wetlands areas have been identified along both the Woman Creek and South Interceptor Ditch
drainage areas. These drainages collect surface water upgradient from OU 2 and deliver the water to pond
Co2 for treatment. Evenly-spaced drop structures along the South Interceptor Ditch have lowered flow
velocities, increased sediment accumulation, and created fair1y dense linear stands of wetlands. From a point
SURFACE WA'TC~ INTCRIIoi REloIeow. AC'T1ON PlAN
ROCI(Y ~LATS PlANT. GOI.lJEN. ~ORAOO
~\__\_"UI._.2.mar
.,..,c" ~ 99'
-------
due south of Building 881 and extending to the C-2 Pond. approximately 0.15 acres of wetland are contained
within this portion of the South Interceptor Ditch. Wedand species observed were primarily cattails (greater
-,
than 95 percent predominance), spike rush lEleocharis macrostachva) and bull rush (Scircus americanus). The
wedands function primarily as flow attenuation features with additional minor contributions to wildlife habitat
..
and water quality enhancement. Drainage contribution to the South Interceptor Ditch from OU 2 is minimal.
2.2.7 Historic Sites
The National Historic Preservation Act of 1966 (Public Law 89-665) together with subsequent law
amendments (Public Laws 91-243, 93-54. 94-422, 94-458) provides that all federal agencies implement
programs for the protection of archeological and historical resources.
The 903 Pad. Mound and East Trenches Areas have been highly disturbed over a number of years.
Due to this disturbance and the topographic position of the subject area, the State Office of Archeology and
Historic Preservation has determined that this action will not impact cultural resources (Burney, 1989). An
archaeological and historical survey of the RFP was conducted between July 18 and August 22. 1988. which
determined two sites have potential eligibDity to the National Register of Historic Places. However.
insufficient information currently exists to make this determination. These two sites are located northwest and
southwest of the investigation area and will not be disturbed by the proposed action (Burney, 1989).
2.3
CONTAMINANTS - DESCRIPTION AND SOURCES
2.3.1
Backaround Characterization
In order to facilitate the interpretation of chemical results in non-background areas. a background
characterization program has been implemented to define the spatial and temporal variabnlty of naturally
occurring constituents.
Fieldwork was conducted in 1989. and a draft Background Geochemical
Characterization Report was prepared and submitted to the regulatory agencies on December 15. 1989
SURFACE WATER INTERn.,. REMEOIAL ACT10N F'I.AN
I'!OCI
-------
(Rockwell International. 1989c). The document summarizes the background data for ground water, surface
water. sediments. and geologic materials. and identifies preliminary statistical boundaries of background
..
variabUIty. Spatial variations In the chemistry of geologic materials and water were addressed by placing
sample locations throughout background areas at the Plant. The goal of evaluating temporal variations in water
chemistry has not yet been achieved because at least two years of quarterty data are needed.
'II.
The draft report has been updated by incorporation of analytical data that were unavaDabie in December
1989. including additional rounds of ground-water and surface water samples for which laboratory analyses
were not avaUabie. The information in the draft background geochemical report has been used to preliminarily
characterize inorganic contamination at the 903 Pad. Mound. and East Trenches Areas. The draft report
presents tolerance intervals for surface water, sediment, and various soli lithologies and hydrogeologic units
(ground water); The tolerance intervals are statistical ranges of the background analyte concentrations in the
various media that represent 95 percent of the population with 95 percent confidence. Summary tables of the
upper limits of these tolerance intervals are provided in Tables A-1 through A~ (see Appendix A) for reference.
2.3.2 Ground-Water Contamination
Ground water at the RFP has been monitored since 1986. Wells have been installed throughout the
property and are sampled quarterty. The following discussion is based on the resulting data.
2.3.2.1 Volatne Organic Contamination
Table A-S (Appendix A) presents all volatile organic compounds (VOCs) with concentrations that are
above detection limits in the unconfined ground-water system during the second quarter of 1989. These are
the most recent validated data pertaining to the same season for which the background levels were
determined. Maximum concentrations of volatile organics based on the complete data set (1986-1989
sampling) are summarized in Table A~. The primary volatile organic ground-water contaminants (CCI.. PCE,
SURF "ce WATER IN'TERIM REMEOIAL. .t.CT1ON PI.AN
~I(V ~......;S
-------
and TCE) are portrayed with isopleths in Figures 2-8 through 2-10 based on second quarter 1989 data for both
unconfined alluvial and bedrock wells.
..
The data In Tables A-5 and A-6 confirm the relative dominance of CCI., PCE and TCE in alluvial and
.
shallow bedrock ground water at OU 2 compared to other volatile organic compounds. and documents
occurrences of 1,1 -oIT. GOUJEN. COlO~DO
89&9'.-,- _"UI._'2."'8I
Ma~c:~ ';s'
-------
EXPLANATION
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EXPLANATION
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SITE (IHSS)
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UN[ OF EQUAL PeE CQNCEMTRA110N (pg/I)
!WHD WHERE APf'ftOXlW.m.y LOCATED
..
or
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03986
o
2587 . BEDROQ( WONrTCR WEll
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CONTOUR INtmt'Al . 20'
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./
U.S. DEPARTMENT Of ENERGY
Rocky flats Plant
Golden, Colorado
OPERABLE UNIT NO.2
SURfACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
fiGURE 2-9
TETRACHLOROETHENE ISOPLETHS
fOR THE UNCONFINED GROUND-WATER
FLOW SYSTEM
Second Quarter 1989
_ch. 1991
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EXPLANATION
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IHDMDUAL ~ SUBSI'~
SITE (1HSS)
..
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LINE OF EQUAl TCE CONCENTRA11OH (N!)
DASHED WHERE APPftOXM\TELY 1.OCA'ItD
-or
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TCE CONCENTRATION ~)
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2587 . BEDROQ( WONITOR WEll
3789 ° AI.LI.MAI. WONITOR WELL
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- - - - - - ~
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Scale: 18 = 600'
rr 300' 800"
I I I
- CONTOUR IHTB\VAL - '1IJ'
0678
1Jllr
u.s. DEPARTMENT OF ENERGY
-. ' Rocky Flats Plant
-~-.'.- .~ Golden, Colorado
-
OPERABLE UNIT NO.2
III) C-2 SURFACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
FIGURE 2-10
- TRICHLOROETHENE ISOPLETHS
-.- -'~ FOR THE UNCONFINED GROUND-WATER
1 - -
-""' ..: FLOW SYSTEM
Second Quarter 1989
-------
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Aluminum. antimony. arsenic. barium. cadmium. chromium, copper, iron. lead, lithium, manganese.
mercury, molybdenum. nickel. potassium. selenium, silver, strontium, vanadium and zinc exceeded background
..
in one or more wells in the second quarter of 1989. Table A-8 (Appendix A), a summary of multiple sampling
events (up to fourteen samples collected from each well during 1987-1989). shows that only a subset of these
analytes repeatedly exceed background (upper limit of the tolerance interval) and/or exceed background by
a wide margin. The sporadic exceedances of background. and the absence of apparent gradients in metal
concentrations with respect to IHSSs. hinders drawing definite conclusions as to whether these constituents
are derived from IHSSs (EG&G. 1990a). Section 2.3.5 makes reference to this and other ambiguities in the
ground-water chemistry data to the extent that they may be relevant to the Surface Water 1M/IRA Plan.
Radionuclides
Table A-9 (Appendix A) shows that dissolved concentrations of the uranium isotopes (U-234, U-235,
and U-238). plutonium, and americium have been above background at OU 2. The maximum concentration
for uranium 238 was 28 % 2 pCl! t in well 12-87 in the 903 Pad Area. Numerous occurrences of uranium at
lower concentrations and in wells completed in diverse lithologies demonstrate that the distribution of uranium
is not thoroughly delineated at OU 2. With respect to plutonium and americium. results at wells 15-87 and 1 1 .
87 were the most elevated (plutonium 0.522 % .117 pCij t and 0.199 % 0.07 pCij t. respectively: americium
0.831 % 0.148 pCitl and 0.06 % .05 pCijl. respectively).
2.3.3
Soil Contamination
The extent of soil contamination at the 903 Pad. Mound. and East Trenches Areas was determined from
soil samples collected in 1987 during the Phase I RI. Samples were collected from boreholes drilled in and
adjacent to known IHSS locations (Figure 2-11). Two-foot intervals were composited for organic analyses. and
two- to ten-foot intervals were composited for all other analytes. Boreholes were not drilled into sites still
';~~1
SUO\F .ce w.-rEf': 1110 "TeAlM O\EMEOIAI. AC110N P\.AN
~I(V "LoAiS I>!..A"''':'. OOL.:)eN. COL:JRAOC
.;&; ."I~&C .,.,n~ '18C.2.mar
ML'C" . 9~'
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'....~'
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-------
EXPLANATION
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o IIH3087
BOREHOLE LOCATION AND
SOIL SANPLE SITE
(REFER TO TABLES 1-.-10 'THROUGH
1-.-13)
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u.s. DEPARTMENT OF ENERGY
Rocky Flats Plant
Golden, Colorado
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OPERABLE UNIT NO.2
SURFACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
FIGURE 2-11
SOIL SAMPLING
LOCATION MAP
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containing wastes (the trenches and 903 Pad) due to potential health hazards to field workers and potential
for release of waste constituents to the environment. The soils data are summarized here because of the
...
potential influences contaminated soils may have on surface water quality. Either direct contribUtions via
overtand runoff, or direct influences via ground-water interactions are possible. The discussion is considered
.
preliminary because wastes were not directly sampled and soils data are still being evaluated.
VOCs. including PCE, TCE, toluene, 2-butanone, CCI.. acetone and methylene chloride, were reported
in samples from the 903 Pad and East Trenches Areas (see Table A-10). Occurrences of total xylenes,
ethyl benzene and toluene were also reported for the 903 Pad Area, whereas 1-2-dichloroethane (1.2-DCA),
1,1,1-TCA. and 1,1.2-TCA were reported in an East Trenches borehole. The Mound Area, like other portions
of au 2, contained acetone (hundreds of pg/1) and methylene chloride (typically tens of J.lgi I) at
concentrations too low to unambiguously demonstrate contamination with these compounds. Other organic
constituents in the Mound Area (PCE. CHCl3. 1,2-DCA) were less numerous and at lower levels than at other
areas within OU 2. Semi-volatile organic compounds di-n-Butyl phthalate, bis(2-Ethylhexyl) phthalate, and N-
nitrosodiphenylamine were detected in numerous boreholes throughout au 2 (see Table A-11, Appendix A).
Several metals occurred above background in soil samples (aluminum, arsenic. barium, cadmium,
calcium, iron. mercury, manganese. lead, antimony, vanadium and zinc). although most exceeded background
by less than a factor of two and/or in only one or two samples. Table A-12 (Appendix A) presents maximum
metal concentrations in soils.
Plutonium a~ americium are the principal radionuclide contaminants exhibiting elevated concentrations
in soils. Table A-13 (Appendix A) presents maximum radionuclid~ concentrations in soils at au 2. Highest
concentrations occurred in samples that included the surface. Because many of the surface soil samples were
mixed into large composites, the Phase I RI data do not rule oUt the presence of radionuclides other than
plutonium and americium. Cesium-137, tritium, and uranium were detected, albeit at near-background
concentrations and in fewer than ten samples. Surface contamination of soils with plUtonium and americium
was further demonstrated by a recent aerial radiological survey (EG&G, 1989). The radioactivity detected in
SURF ACE W A 'TEl'! IN'TCRIM REMEDIAl. ACTION F'\.AN
CICCI<" <~.5 "\.AN". GO\DEN. COI.ORAOO
eog&; ""'.raD walt'lIft'MC.2.mar
Ma:," .~S.
-------
that survey was associated with known radioactive material storage and handling areas (Le., the 903 Pad), and
was attributed to plutonium. americium, and a uranium decay product. The survey indicated elevated
IT
concentrations of americium in soils east of the 903 Pad Up Site as high as 97 pCijg, and by inference from
their expected activity ratio, plutonium as high as 500 pCijg. Subsequent analysis of samples from the area
..
with high americium concentrations indicated plutonium concentrations as high as 457 pCi/g. The cesium-137
activity was at a level consistent with global fallout and not enriched in the Plant area.
2.3.4 Sediment Contamination
Sediments in Woman Creek and South Walnut Creek were sampled in the fall of 1986, and in March
and October of 1989. Stations SED-28, SED-29. and SED.25 are located within the South Interceptor Ditch
in the Woman Creek drainage (Figure 2-12). SED-30 and SED-31 are seeps on the South Interceptor Ditch
berm near station SED-29. SED-27 and SED-26 are along Woman Creek just upstream of Pond C-2. Stations
SED-11, SED-12, and SED-13 are located along South Walnut Creek. SED-11 is the most upgradient station,
SED-12 is just upstream of Pond 8-1, and SED-13 is just downstream of Pond 8-5. Stations SED-1 and SED-2
on Woman Creek and an ephemeral tributary, respectively, are both downstream of OU 2, just west of Indiana
Street within the boundary of the buffer zone (east of area depicted by Figure 2-12).
2.3.4.1 Woman Creek Drainage
VOCs were detected in samples from the sediments in the Woman Creek drainage (Table A-14,
Appendix A). Chloromethane was present at SED-29 (SO pg/kg), and chloroform was reported at SED-31 (18
pgjkg). Several sediment samples contained methylene chloride and acetone at very low concentrations.
These compounds were frequently found in associated blanks. SED-30 contained 220 pg/kg acetone at one
sampling, but acetone was also present in the blank for this sample and was undetected in two other sampling
events for this station in 1989. Acetone and methylene chloride results in this area are believed to be
laboratory artifacts. The only other volatile organic compounds detected in the Woman Creek drainage
sediment samples were TCE (8 pgjkg) at SED-31 (estimated below detection limits elsewhere), and toluene
estimated below detection limit at SED-29 and SED-3D.
Su~.o.ce w.o.,,!> 1~~101 ~IoIEDIA... .o.C"10N "LAN
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-------
EXPLANATION
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INDMDUAL HAZARDOUS SUBSTANCE
SrrE (IHSS)
.lI
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Scale: 1. = 600'
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CONTOUR INTERVAL. .. 7Sf
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u.s. DEPARTMENT OF ENERGY
Rocky riots Plant
Golden, Colorado
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OPERABLE UNIT NO.2
SURFACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
FIGURE 2-12
SURFACE WATER AND SEDIMENT
MONITORING STATIONS
-=:-
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Of the metals, beryllium, lithium, silver, tin, and zinc were notably elevated above background in the
~
sediment of the South Interceptor Ditch and Woman Creek (Table A-15, Appendix A). Concentrations of silver
(as high as 49 mg/kg) are greater than five times the upper limit of the background range at stations SED-25.
SED-26. and SED-30. Beryllium was not detected in the background samples « 1.1 mg/kg) but occurs at
"
concentrations ranging from 3.8 to 15.5 mg/kg in all the sediment samples collected from the South Interceptor
Ditch and Woman Creek. Although tin was not above background «22.8 mg/kg) at SED-27, SED-28, and
SED-31, It occurred In a range from 364 to 1080 mg/kg in stations SED-25, SED-26. SED-29, and SED-30.
Concentrations of zinc (as high as 735 mg/kg) are greater than the upper limit.of the background range at
stations SED-11. SED-28, SED-29, and SED-30.
Plutonium was above background at stations SED-1. SED-2, SED-25, SED-26, SED-29, and SED-30,
ranging in concentration from 0.06 to 0.85 pCi/g (Table A-16. Appendix A). Contaminated surface soil from
the 903 Pad Area, transported primarily by wind, may be the source of this plutonium.
2.3.4.2 South Walnut Creek Drainage
The South Walnut Creek sediment monitoring stations include SED-11. SED-12 and SED.13. Only one
sample was obtained from each of SED-12 and SED-13 (13 August 1986). Due to prioritization of sampling
activities. additional samples were not collected from these stations. Table A-14, Appendix A shows that
acetone was reported for all three stations and was also associated with laboratory blanks. SED-11 was found
to contain TCE and 2-butanone at concentrations of 39 mg/kg and 12 pg/kg, respectively. All other VOCs
were either not detected or reported below detection limits for SED-11. SED-12 and SED-13.
As in the Woman Creek drainage, beryllium, lithium, silver. and tin are elevated in the sediments at
SED-11. They occurred at concentrations of 2.5.7.2, 15.0. and 404 mg/kg, respectively. Zinc was also notably
elevated, occurring at a concentration of 735 mg/kg (the upper limit of the background tolerance interval is
93 mg/kg). Uranium 235 was reported at a concentration of 0.2 pCi/g for SED-11 and americium levels were
reported at 0.19 pCi/g and 0.03 pCi/g for SED-12 and SED-13. respectively. Plutonium was also found at a
SURF lice WATER II'lTCRIfoot REMECMI. IICT10N "'-AN
~ o:";>'"!"S "~Ni. GOI.OE". COLORA:JO
erg&.; ."'I"-P' ..,n~ ,..co2.maI
Mate,. '99'
-------
concentration of 0.35 pCi/g at SED-12. Wind~ispersed contaminated soils from the 903 Pad and Up Area may
be the source of these radionuclides.
?
2.3.5
Surface Water Contamination
.~
Twenty-six surface water and surface seep stations in the vicinity of the 903 Pad. Mound. and East
Trenches Areas were sampled during field activities from 1986 through 1990 (see Appendix B). The following
discussion is based on all avaUabie data because many seeps or stream stations were dry during some
samplings. These data have been summarized in Appendix C and compared to ARARs (see Section 3 for
ARAR identification). Total radiochemical and metals data. although presented in the Appendix, are not
discussed because an assessment methodology that accounts for varying concentrations of suspended solids
is still being developed. Surface water monitoring locations are shown on Figure 2-12.
Flowing surface water in drainages was sampled at stations on the South Interceptor Ditch and Woman
Creek just upstream of Pond C-2 and at stations upstream of the B-series ponds on South Walnut Creek. The
B-series ponds were not sampled for this investigation. as they will be subsequently investigated as part of
another operable unit.
The surface water seeps are downslope and southeast of the 903 Pad Area. and downslope and north
of the Mound Area and East Trenches Areas. Because surface water at seeps and in streams represents
ground-water discharge (intermittent discharge with respect to streams). the surface water compositions are
similar to those of local ground water. The data for both media show that PCE. TCE. CCI.. and their
degradation products are the principal VOCs. and they show very similar major ion contents as well. However,
there is enough variability within stations so that it is not possible to demonstrate surface/ground-water
connections on a well-by-well. seep-by-seep basis.
SU~ACE WATEF> Ip.nc~", REMEOIAL. ACnoN PlAN
'!OCI(V F~TS "'LA"";. GOLOE"'. COLOAADO
I'Q&; .~lr&D -.Jr'''J' .~.2.mar
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-------
2.3.S.1 Surface Water Stations Southeast of 903 Pad Area
".
There are several seeps downslope to the southeast of the 903 Pad. Surface water stations established
.J.
at these seeps in the 903 Pad Up Area are designated SW-SO, SW-S1, SW-S2, SW-SS, SW-S7, SW-S8, and
SW-77. Station SW-SO is closest to the 903 Pad, and SW-S7 and SW-S2 are south of SW-SO. SW-S1 and
SW-S8 are located in a ditch along the road east of SW-SO; however, overland flow of seepage from SW-SO,
SW-S2, and SW-S7 will also enter the ditch. Water in the ditch passes under the road south of these locations
through a. culvert. The discharge of the culvert is sampled at station SW-SS. SW-77 is another seep located
on the east side of the road, just north of SW-SS. It is noted, therefore, that SW-S1, SW-S8. and SW-S5 are
physically connected and likely receive flow from SW-SO, SW-S2. and SW-S7. Farther downgradient stations
include seeps at SW-53 , SW.02. SW~, and SW-&4; SW-27, SW-30, SW-S4. and SW-70 on the South
Interceptor Ditch; and SW-26. SW-28. and SW-29 on Woman Creek.
Data for seeps in the vicinity of the 903 Pad Up Site and farther downgradient at SW-S3, SW-63, and
SW-&4 indicate organic contamination. Contaminants in seeps in the vicinity of the 903 Up Site include 1,1.
DCE. 1.2-DCE. CCI.. TCE, and PCE, with concentrations of CCI. and TCE exceeding 1000 JJg/ t. Occasionally
1.2-DCE and TCE are present at SW-53. low concentrations of 00. and TCE «20 JJg/ t) occur at SW-63, and
low concentrations of TCE occur at SW-&4. Methytene chloride also occasionally occurs in these seeps. but
at concentrations near the detection limit, and frequently also occurs in the laboratory blanks. Low and very
infrequent concentrations of these and other VOCs occur at seep SW..o2 as well as at stations along the South
Interceptor Ditch. The water-quallty data for stations along the South Interceptor Ditch and Woman Creek do
not provide unambiguous evidence of contamination; however, the VOC concentrations in the upgradient seeps
suggest that a solvent plume within alluvial ground water is migrating to the southeast, which is consistent with
the alluvial ground-water flow direction. It is inferred that VOC contaminated alluvial ground water approaches
the South Interceptor Ditch and Woman Creek.
With respect to inorganic and dissolved radionuclide contamination. there are somewhat elevated
concentrations of TDS, major ions, aluminum, strontium, zinc, and uranium at most of these stations. Unlike
SU~ACE WATER INTERIM REMEDIAL ACTION PI.AN
ROO
-------
the absence of VOCs in surface water at stations along the South Interceptor Ditch (SW-70, SW-30, SW.54,
and SW-27), all have somewhat elevated uranium concentrations (generally less than 10 pCi/1 of total
uranium). These concentrations are usually above ARAR (5 pCi/1). Although the 903 Pad Area cannot be
~
ruled out as the source of the uranium, the occurrence of elevated uranium as far upgradient as SW-70
suggests the 881 Hillside Area as a potential source. Alluvial ground water at the 881 Hillside contains levels
.\.
of uranium above background.
Seeps in the vicinity of the 903 Pad Up Site (SW-SO, SW-53 , and SW-54) had detectable plutonium
and/or americium during one sampling event in 1989 (two events for SW-53). The samples contained
substantial suspended solids and were not filtered at the time of collection, and surface soils in the vicinity of
the seeps are contaminated with radionuclides. Furthermore. total radiochemistry data do indicate notably
higher plutonium and americium concentrations than in filtered samples. demonstrating that most of the
radionuclides are in a particulate form. Therefore, the local soils represent the most direct potential source for
seep contamination. However, there were traces of plutonium in a few ground-water samples (highest
concentration at well 15-87, 0.522 : 0.117 pCij 1) so ground water is also a potential source of radionuclides
in seeps, albeit a less significant one.
It Is noted that plutonium and americium are essentially insoluble in natural waters, but they can migrate
in colloidal form. and colloidal-size particles can pass through 0.45 pm filters such as those used in the
previous investigation (Puis and Barcelona. 1989). The DOE is currently conducting a study to assess the
distribution of plutonium and americium in surface water with respect to suspended solids particle size. The
study will include filtration of surface water through three pore sizes, and laboratory analysis for plutonium and
americium in the filtered and unfiltered fractions «0.10 pm, 0.10 #1m to <0.20 #1m, 0.20 #1m to <0.45 pm, and
2. 0.45 pm). Although this study was not explicitly designed to differentiate colloidal and dissolved
radionuclides, and therefore will be unable to quantify colloidal material under 0.' #1m, it will demonstrate
whether a significant portion of the radionuclides are between 0.' and 0.45 pm and thereby provide some
indication of the Importance of colloidal transport. Also, if most of the plutonium is particulate in nature
(>0.1 pm in size), it is likely plutonium can be removed from surface water by unit processes effective at
removal of suspended solids, e.g., sedimentation and filtration.
SUI'IFACE WATEFI INTE~"" l'IE""EOIAl AC'T1ON P\.AN
~ .!.A~S ~..AN". GOLDEN. COLOFlAOO
~; .""II'8Q~W8.Inlol1.M<.2.mar
Marc'" ~99'
-------
Regardless of the transport mode. total plutonium concentrations occur above background at station
..
SW-29 on Woman Creek (range:
-------
South Walnut Creek Basin surface water, as characterized by data for stations SW-56. SW-59, SW~,
SW-61. and SW-101. contain 004, PCE, and TCE in concentrations in excess of 200 pg/I. with lesser and
...
infrequent concentrations of 1,1-DCE. 1,1-DCA, 1,2-DCE, vinyl chloride (all are possible degradation products
of TCE and PCE), acetone, bromo-dichloromethane, and methylene chloride. The latter compounds may be
.1.
contaminants, but the data do not allow this conclusion to be drawn with certainty. These stations also
frequently have surface water concentrations above ARARs for TDS and uranium. The TDS and uranium
concentrations are typical of the alluvial ground water in the vicinity of the 903 Pad and Mound Areas. CCI.,
PCE, TCE-, and elevated zinc are also present in the alluvial ground water at the Mound Area.
The only datum available for Station SW-23 (August 1986 sampling) shows an absence of VOCs.
Although there are no August 1986 data for the upstream stations, the data suggest the organics have
volatilized over this reach.
2.3.5.3 Seeps at the East Trenches Areas
Of the two seeps at the East Trenches Areas (SW-65 and SW-103), SW-65 has no apparent organic
contamination, and SW-103 has the constant presence of CCl4 at concentrations less than 10 JJg/ I. Dissolved
uranium was also above ARAR at SW-65. Uke the 903 Pad and Mound Areas, the chemistry of these seeps
is similar to the localized ground water.
2.3.6
Air Contamination
The 903 Pad Area is recognized as the principal source of airborne plutonium contamination at the RFP.
An extensive air monitoring network known as the Radioactive Ambient Air Monitoring Program (RAAMP) is
maintained at the Plant in order to monitor particulate emissions from the 903 Pad Area and other Plant
facilities. Historically, the particulate samplers located immediately east. southeast. and northeast of the 903
Pad. Mound, and East Trenches Areas have shown the highest plutonium concentrations. This finding is
corroborated by the results of soil surveys which indicate elevated plutonium concentrations to the east.
SU""'ACE WATE'" INTE""101 REIoIEOIAl, AC'TION PLAN
~K" ~t..'o~S ~..AN". GOL.DE~ COI.:>I'IAOC
.; ~Ira.c ~n\Jt MC-2."'8I
"'.rcP'\ ~ 99'
-------
..
particular1y southeast of the area. However, RAAMP has found ambient air samples for plutonium to be well
within the DOE guidelines of 20.0 x 10" pCi/ I established for the protection of human health (Rockwell
International. 1987b).
..
2.3.7 Summarv of Contamination
The Phase I RI investigations of environmental media lead to the general conclusions that volatile
organic aAd radionuclide contamination exists in solis. surface water and ground water around several au 2
IHSSs. and that the distribution and magnitude of the contamination can be better delineated via sampling and
analysis planned for the Phase II investigation.
TCE. PCE and ca. are the principal organic contaminants in surface and ground waters. with lesser
amounts of their degradation products and other compounds at numerous sampling sites throughout au 2.
Plutonium and americium In surface water samples are other apparent Indicators of RFP~erived contamination.
Several metals and other inorganic constituents (including uranium) are also above background in the
environmental media. but the data do not permit unambiguous conclusions with regard to contamination. The
uncertainty results in part from the absence of clear concentration gradients and from the limited knowledge
of the inorganic composition of waste sources in OU 2. Natural processes (e.g.. evaporative concentration)
may govern the source and distribution of such inorganic constituents. This will be further investigated in the
context of long-term remediation at OU 2.
2.4
ANALYTICAL DATA
Organic. inorganic and radionuclide contaminants exist in au 2 surface water. Volume II (Appendix B)
presents a compilation of volatile organic. inorganic and radiochemistry data for all surface water stations at
au 2 that are available at this time. Only a small fraction of the data have been validated; they are identified
in the appendices by a qualifier adjacent to each datum. The qualifiers "V' (valid), "A" (acceptable with
SURF ACE W A TEFl II'lTEFIIM F!EMEOIAL AC110N PlAN
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a.Aa.r:r- 199"
-------
qualifications). and "R" (rejected) are assigned in accordance with the ER Program Quality Assurance/Quality
Control (QA/QC) Plan (Rockwellintemational. 1989b). Rejected data either did not conform to the QA/QC
"
procedures. or insufficient documentation exits to demonstrate conformance with these procedures. These
data. at best. can only be considered qualitative measures of the analyte concentrations. The schedule for the
1M/IRA does not permit waiting for all data to be validated. However, the validated data and their similarity
'-
to unvalidated data are considered sufficient to justify and to define the general configuration of the 1M/IRA.
2.5
SITE CONDITIONS THAT JUSTIFY AN 1M/IRA
As discussed in Section 1, there is no immediate threat to the public health and environment posed by
surface water contamination in South Walnut Creek Basin. The affected surface water is contained within the
plant boundary by existing detention ponds. and is treated and monitored prior to discharge. There is,
however, potential for an imminent threat to develop and implementation of this 1M/IRA will reduce the
likelihood that such a threat will result by enhancing DOE's efforts to manage contaminated surface water.
Although downstream safeguards are provided by the B-Ponds, this 1M/IRA should reduce the potential for off.
site migration and uncontrolled releases of contaminated surface water by reducing contaminated surface water
loading to the Ponds. In addition. by collecting contaminated surface water through diversions at the sources,
this 1M/IRA will mitigate downstream migration of contaminants and could reduce the size and cost of future
RFP remedial actions. Such an action is consistent with the goals for a final remedy at the site.
This 1M/IRA focuses only on controlling the migration of hazardous substances in South Walnut Creek
Basin surface water and does not address soil or ground-water contamination. An au 2 Phase II RI Plan has
been prepared to further characterize the extent of contamination in preparation for further remedial actions
at OU 2.
SUR~ACE WA':'E" INTeR!"" REtoAEDlAI. ACT10N PlAN
~I('V °:..A.S P:.,A>r GOL.:)E'/. COL:>AADC
89&; ""I!&C 'IIW&In~ MC..~.rna:
U&rCI"l196'
-------
~
A
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SECTION 3
IDENTIFICATION OF INTERIM REMEDIAL ACTION OBJECTIVES
..
3.1
SCOPE OF INTERIM MEASURES/INTERIM REMEDIAL ACTION
..a
The overall objective of the South Walnut Creek Basin 1M/IRA at OU 2 is the mitigation of downgradient
contaminant migration within surface water by means of the collection and treatment of contaminated surface
water to ~chieve, to the extent practicable, ARMs (see Section 3.3). ARARs are used in defining the
remediation goals for the Interim action. Based on the meetings between DOE, COH, and EP A during February
and March 1990, and comments received during the public comment period, DOE is proposing this 1M/IRA
Plan which specifies point source locations for the collection of contaminated surface water, and provides for
the collection and treatment of flows exclusive of those resulting from high precipitation events.
3.2
INTERIM REMEDIAL ACTION SCHEDULE
Revisions to this plan based on public comment, preparation of a Responsiveness Summary pursuant
to the public meeting, treatabDIty studies, and design and implementation of this 1M/IRA will occur through
Spring 1991. MDestone dates for specific activities are presented in Table 0-', Appendix O. Table 0.' shows
the milestone schedule as proposed in the draft FFACO/IAG (DOE, 1990a).
3.3
COMPUAN9E WITH APPUCABLE OR RELEVANT AND APPROPRIATE REQUIREMENTS (ARARs)
AND PROTECTION OF HUMAN HEALTH AND THE ENVIRONMENT
The NCP [FR Vol 55, No. 46, 8848; 40 CFR 300.430 (e)] requires that, in development of alternatives
for final remediation, the following be considered:
1.
ARARs;
2.
for systemic contaminants, concentration levels that will not cause adverse effects to the human
population and sensitive subgroups over a lifetime of exposure;
SU!'!FACE WAre!'! INTERIM I'IEMEDtAL ACTION P\.AN
I'!OCI('V F'-"'~ "'-ANT. GOI..DEN. COLOI'\ADO
819&; ~'/'UI. -..nU!. 88C:-3.m&r
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-------
3.
for carcinogens. concentration levels that represent an excess lifetime individual cancer risk less
than 10" considering multiple contaminants and multiple pathways of exposure:
4.
factors related to detection limits;
...
5.
for current or potential sources of drinking water, attainment of Maximum Contaminant Level
Goals (MCLGs) or Maximum Contaminant Levels (MCLs), if MCLGs are zero: and,
..
6.
attainment of Oean Water Act (ONA) water quality criteria where relevant and appropriate.
The lAG. in paragraph 150. states "Interim Remedial Actions/Interim Measures shall. to the greatest extent
practlcabte, attain ARARs." Also for Interim actions, the NCP [40 CFR 3OO.430(f)] specifically notes that an
ARAR can be waived if the action is to become part of the final remedy that will attain ARARs. The results of
the treatability studies identified in Section 6.4 will allow evaluation of the extent to which the 1M/IRA will attain
ARARs. I.e.. It may not be practicable to attain all ARARs for this Interim action and ARAR waivers or altemate
concentration limits may be requested after the study is completed.
This section identifies and analyzes ARARs relevant to the South Walnut Creek Basin 1M/IRA and
discusses how the action will be protective of human health and the environment. This remedial action is
considered an on-site 1M/IRA to be administered under CERCLA; therefore. only substantive and not
administrative requirements of regulations (such as RCRA) apply. Permits. for example. are not required (per
paragraph 121 of the lAG).
"Applicable requirements," as defined in 40 CFR 300.5. means "those cleanup standards. standards of
control, and other substantive requirements. criteria. or limitations promulgated under federal environmental
or state environmental or facility siting laws that specifically address a hazardous substance, pollutant.
contaminant. remedial action. location, or other circumstance found at a CERCLA site. Only those state
standards that are identified by a state in a timely manner and that are more stringent than federal requirements
may be applicable." "Relevant and appropriate requirements: also defined in 40 CFR 300.5. means "those
cleanup standards. standards of control. a.nd other substantive requirements, criteria. or limitations promulgated
under federal environmental or state environmental or facility siting laws, that, while not "applicable" to a
hazardous substance, pollutant, contaminant. remedial action, location, or other circumstance at a CERCLA
S;;R~ACE WATE'" INTERlt.I ~t.lEDIAL AC1'10N !>\AN
ROCI(V .";'.5 "'..A"". GOI...:>E",. CO\.OI'\ADO
e>g&; ..,.,ra= ....,nlJ: MC.:'.1"t'\&f'
MatC"" '9S'
-------
site, address problems or situations sufficiently similar to those encountered at the CERCLA site that their use
is well suited to the particular site. Only those state standards that are identified in a timely manner and are
..
more stringent than federal requirements may be relevant and appropriate." In addition to applicable or
relevant and appropriate requirements, advisories. criteria, or guidance may be identified to be considered
.#
(TSC) for a particular release. As defined in 40 CFR 3oo.4OO(g)(3), the "to be considered" (TSC) category
consists of advisories, criteria. or guidance developed by EPA. other federal agencies. or states that may be
useful in developing remedies. Use of -rSCs" is discretionary rather than mandatory as Is the case with
applicable. or relevant and appropriate requirements.
In general. there are three categories of ARARs. These categories are:
.
Ambient or chemical-specific requirements
.
Location-specific requirements
.
Performance, design. or other action-specific requirements
Each category is discussed in more detail below.
3.3.1
Ambient or Chemical-Scecific Reauirements
Ambient or chemical-specific requirements set health- or risk-based concentration limits in various
environmental media for specific hazardous substances or pollutants. These requirements set protective clean-
up levels for the chemicals of concem in the designated media. or indicate a safe level of air emission or
wastewater discharge. The chemical-specific ARARs identified herein are used in defining the remediation
908ls for clean up of contaminated surface water and discharge of treated water.
ARARs are derived primarily from federal and state health and environmental statutes and regulations.
The following may be considered when establishing clean-up standards, but are not considered ARARs: Health
Effects Assessments. Health Advisories, Chemical Advisories, and Guidance Document criteria. These and any
SURFACE WATER INTERIM REMEDIAl ACTION PLAN
ROCKY FLATS PlANT, GOLDEN, COLORADO
eg&9\ -.irap \walnul\88C.3.mar
March 1991
-------
proposed standards are classified as items to be considered, or TBCs. Where background concentrations for
constituents are above the ARAR for that constituent. a waiver from the ARAR may be appropriate. A summary
.
of ARARs for the contaminants found in South Walnut Creek Basin surface water at au 2 are presented in
Appendix E, Tables E-1.1 through E-1.4. Tables E-1.1, E-1.2, E-1.3, and E-1.4 present ARARs for volatile
organics, metals. conventional pollutants, and. radionuclides. respectively and will be applied to operations
~.
involving water treatment effluent.
As"discussed in 55 FR8741, when more than one ARAR has been Identified for a contaminant, the most
stringent standard has been Identified as the ARAR which the 1M/IRA will attain to the greatest extent
practicable. Where no ARAR standard exists, a TBC standard has been identified which the 1M/IRA will treat
as a goal to achieve.
An ARAR analysis for volatile organics. metals. conventional pollutants. and
radionuclides. respectively. is presented in Tables E-2.1. E-2.2, E-2.3. and E-2.4. The screening process
includes consideration of both ground-water and surface water standards because of the p."ooable interaction
of alluvial ground water and surface water in the drainages of the RFP. Of the elements/compounds detec!ej
in South Walnut Creek Basin surface water at au 2, there are no ARARs for calcium, magnesium, potassiur:.
sodium, bicarbonate, and strontium.
However. the TDS ARAR establishes the acceptable aggregate
concentration for the above major ions (excluding strontium). Although no ARAR or TBC exists for strontium,
an objective of this 1M/IRA will be to reduce strontium to background levels.
3.3.1.1 Safe Drinking Water Act Maximum Contaminant Levels (MCLs) and MCL Goals
Because South Walnut Creek Basin surface water at au 2 is a source of drinking water, MCLs are
relevant and appropriate for all phases of the 1M/IRA. MCLs are derived from the Safe Drinking Water Act
(SDWA) (PL 93-523). They represent the maximum permissible level of a contaminant in water which is
delivered to the free-flowing outlet of the ultimate user of a public water system [40 CFR 141.2(C)). Per the
new NCP. MCLGs have also been considered in developing clean-up standards.
SUOU'ACE WATO;I:I II'lTERI... I:IE"'EOIAI. ACT10N PLAN
!:lOCI(" ~;..US "LAN1'. GOI.DEN. COI.ORADC
~; ...,.,rap .W8JnU't. MC.3.rn&I
~a':~ '9~'
-------
3.3.1.2 Ambient Water Quality Criteria
~
The Ambient Water Quality Criteria (AWQC) are non-enforceable guidance developed under the CWA.
Guidance is set for surface waters for the protection of aquatic life and for the protection of human health.
..
based on consumption of both drinking water and aquatic organisms from that water. The proposed 1M/IRA
involves treatment and discharge to surface water that has a use-protected designation. aquatic life Class II
warm water classification. Although not ARAR, per the new NCP, the AWQC are considered as relevant and
appropriate preliminary remediation goals. Final remediation goals wUI be set according to ARARs and for total
risk due to carcinogens that represent an excess upperbound lifetime cancer risk to an individual to between
10" to 1 0041 lifetime excess cancer risk when the final remedy is selected for all of OU 2.
3.3.1.3 Colorado Surface and Ground-Water Quality Standards
The Colorado Water Quality Control Commission (WQCC) has proposed ground-water quality standards
for many compounds for protection of both human health and agricultural uses. These proposed standards
are considered TeC since they are not enforceable standards untO RFP's ground water is classified by the
WQCC. Where standards exist for both human health and agricultural uses. the more stringent standard is
selected as TBC.
Permanent surface water quality standards have been adopted by WQCC for Walnut Creek. These
include standards for many organic. inorganic and radionuclide parameters. These standards went into effect
March 30. 1990. and are considered applicable to this interim remedial action.
For both ground water and surface water standards. some of the standards are lower than the current
standard detection limits for the constituents. When this occurs. the WQCC Practical Quantitation Umit (POL)
will be considered as the ARAR.
SURFACE WA~R IN'TCAIIooI REIooIEOIAL AC'T1ON PI.AN
~ ~:...ATS "'..ANT. GOlDEN. COI.OI'IAOO
~g,_,_._n"",_'J.mar
Marc'" 199'
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3.3.1.4
RCRA Ground-Water Protection Standards
-.
Owners or operators of facilities that treat. store, or dispose of hazardous waste must ensure that
hazardous constituents listed in 6 CCR (Colorado Code of Regulations) 1007-3 and 40 CFR 261. Appendix VIII,
entering the ground water from a regulated unit do not exceed concentration limits under 6 CCR 1007-3 and
40 CFR 264.94. The concentration limits include standards for 14 compounds. with background' or alternate
.
concentration limits (ACLs) , used as the standard for the other RCRA Appendix VIII constituents. These
concentrat~on limits apply to RCRA-reguJated units subject to permitting Oandmls. surface impoundments. waste
piles, and land treatment units) that received RCRA hazardous waste after July 26, 1982. Although this area
does not contain RCRA-regulated hazardous waste management units. it does contain IHSSs. As a result,
these RCRA (Subpart F) regulations are considered relevant and appropriate for ground water remediation.
These requirements are not applicable or relevant and appropriate with respect to the proposed interim
remedial action in that they do not specifically address the collection. treatment, and discharge of surface
waters nor are these activities sufficiently similar to the circumstances regulated by the RCRA Subpan F
requirements to be relevant and appropriate. RCRA ground-water protection requirements relate specifically
to protection against degradation of the uppermost aquifer by a regulated unit, or a solid waste management
unit (SWMU) in the case of Corrective Action activities. which clearty do not relate to the collection, treatment.
and discharge of surface waters. whether or not such waters have been affected by the introduction of ground
water through seeps. The RCRA ground-water requirements do provide an effective mechanism for the
protection of the uppermost aquifer and, consequently, potential drinking water sources. Accordingly. since
- ..
effluent discharges could potentially affect downstream drinking water sources, the Subpart F requirements
have been included as TBC for surface water. Background concentrations for 40 CFR 264. Appendix IX
constituents not listed in Appendix VIII are also TBC for surface water.
TBC background surface water values for RCRA Subpart F are applied u$ing maximum concentrations from background surface
water at RFP.
SURFI.CE WA~C\ 'I'lTERlt.I !'IEt.lEOIAl. ACT10N PlAN
'lQC1(V .i...US PlAN'. GOt..:>EN. CO\.OAAOO
eg&S~"'t~'W8in"" . 88C.3.mat
Marc" '9S'
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3.3.1.5 Protection of Human Health and the Environment
..
As Ulustrated by the hazard quotients and carcinogenic risks listed in Tables E-1.1 through E.1.4,
achieving the ARARs should result in a clean-up action that is protective of human health and the environment.
~.
For non-carcinogens, the protectiveness goal is a hazard index of 1. The hazard index is the sum of the
hazard quotients [i.e., the estimated daily intake (dose) to reference dose ratios) for all of the contaminants
combined, which have been computed and are presented in Table E-1. In assessing non-carcinogenic risk,
a hazard Index of one or less is considered to be acceptable. If the hazard index exceeds one, it indicates
that there might be the potential for adverse non-carcinogenic health effects occurring. Unlike the method
used to evaluate the potential for carcinogenic toxicity, the hazard index does not indicate the probability of
adverse health effects occurring, but it is used as a benchmark for determining where there is a potential
concern. With respect to carcinogens, cumulative cancer risk should be less than 10" (individual cancer risks
shown in Table E-1 are considered additive). As noted in Table E-1, the calculated incremental cancer risks
exceed 10" for some of the organic carcinogens as well as for arsenic and beryllium. However, the cancer
risks are computed on the basis of the detection limit and therefore can only be considered a possible
maximum carcinogenic risk; the actual risk is unknown but likely to be considerably lower. Removing these
contaminants to non-detectable levels and attaining, to the extent practicable, the other ARARs, the 1M/IRA
is considered protective of human health and the environment.
3.3.2 Location-Scecific Reauirements
Location-specific ARARs are limits placed on the concentration of hazardous substances or the conduct
of activities solely because they occur in certain locations. These may restrict or preclude certain remedial
actions or may apply only to certain portions of a site. Examples of location-specific ARARs which pertain to
the 1M/IRA are federal and state siting laws for hazardous waste facilities (40 CFR 264.18, fault zone and
floodplain restrictions), and federal regulations requiring that actions minimiZe or avoid adverse effects to
wetlands (40 CFR Part 6 Appendix A and 40 CFR Parts 230-231).
Si.I~ "CE W" TER INTERIM REr.4ECtAL AC'TlON PLAN
~I(V >IJIoTS PIJIoNT. GOlDEN. COLOAAOO
.g&; ...traQ..,..nu1 MC-3.mar
"'&1("" 1 9S'
-------
More specifically. in addition to the requirements described above, pertinent location-specific ARARs
include: Colorado requirements for siting of hazardous waste facilities and wastewater treatment facilities
)0
(Colorado Revised Statute 25-15-101, 203. 208, 302 and 25-8-292. 702, respectively). National Historic
Preservation Act requirements for preservation of significant articles and historic properties (36 CFR Parts 65
and 800, respectively). federal critical habitat protection requirements (SO CFR Parts 200, 402 and 33 CFR Parts
320-330). and federal requirements for the protection of fish and wUdlife resources (40 CFR 6.302).
~
A $ummary of location-specific ARARs which the 1M/IRA wm attain to the greatest extent practicable
is presented in Table E-4.
3.3.3 Performance. Oesian. or Other Action-SDecific Reauirements
Performance, design, or other action-specific requirements set controls or restrictions on particular
kinds of activities related to management of hazardous substances or pollutants. These requirements are not
triggered by the specific chemicals present at a site. but rather by the particular 1M/IRA alternatives that are
evaluated as part of this plan. Action-specific ARARs are technology-based performance standards. such as
the Best Available Technology (BAT) standard of the Federal Water Pollution Control Act. Other examples
include RCRA treatment, storage, and disposal standards, and Clean Water Act pretreatment standards for
discharges to publicly-owned treatment wort
-------
workers involved In hazardous substance-related activities, as well as other OSHA requirements related to
specific circumstances or activities. These requirements are not environmental in nature, however, and are not
.
to be included as ARARs. Those requirements which are applicable are just that, applicable, while non-
applicable requirements could. at most. be relevant and could be included as guidance to be considered
..
(TSC) .
SURF ACE WATER INTERIM REMEDIAL ACTION ~l.AN
-------
-------
SECTION 4
IDENTIFICATION AND ANALYSIS OF 1M/IRA ALTERNATIVES
..f
4.1
SURFACE WATER COil ~CTlON AND TREATMENT ALTERNATIVES
.
This section presents the technique for collection of contaminated surface water and a detailed
evaluation of alternative treatment technologies. Treatment technologies corresponding to the following
catego~ are evaluated in this section:
.
Treatment for Suspended Solids Removal;
Treatment for Radlonucllde Removal; and
.
.
Treatment for VoiatUe Organic ConstItuent Removal.
The treatment technologies selected for consideration are based on their probability of attaining the
effluent requirements (ARARs presented In Section 4.1.2). The process for critical evaluation of the treatment
technologies is presented in Section 4.2. The evaluation criteria Include effectiveness, Implementability and
cost of the technology. Section 4.3 examines In detal the technique of surface water collection by diversion.
at the sources. The treatment technologies are presented and evaluated in Section 4.4. The treatment system
designs presented In Section 4.4 are conceptual. with only enough detaR to determine relative costs. Detailed
design and costing for the 1M/IRA wli be conducted after the results of the bench and field-scale treatability
studies are obtained. T~ comparative cost evaluations employ a standard 3O-year basis for present worth
analysis. However. the actual service life of the South Walnut Creek Basin Surface Water 1M/IRA is not known
at this time. The 1M/IRA coUd, tor example. become a part of the long-term OU 2 remedial action. Lastly,
all solid waste generated during the 1M/IRA. with the exception of activated carbon (e.g., filter cake, excavated
soils from installation of the surface water diversion and collection structures. and sediments accumulating in
the collection system during operation) will be characterized and handled according to the RFP waste
management operating procedures. For costing purposes, however, It is assumed that these wastes will be
handled and disposed as low-level mixed waste.
SURFACE WATEFlINTERIoI REIoIEDIAi. AC'T1ON PI..AN
RQCI(V ~1..f.TS PI..AHT. GOI..OEN. COLORADO
89&;'."""',.p \-.JnU1 \8IC~."""
Marc" 1991
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4.1.1
Surface Water Collection T echnoloaies
'"
Figure 4-1 Ilustrates the locations of the South Walnut Creek Basin surface water seeps and in-stream
monitoring stations. As mentioned In Section 1.0, general agreement between EPA, CDH and DOE was
reached on the specific locations for collection of contaminated surface water. These locations are designated
.
in Figure 4-1 as the 81M/IRA Surface Water Monitoring Stations8 and Include SW-56. SW-59. SW~, SW~1,
SW-101, and SW-132. It was agreed that flows at these stations would be collected either at the stations or
immediately downstream at a point of confluence. Figure 4-2 offers a detaled plan view of the locations of
SW-59. SW-6). SW~1, SW-132. and SW-133In the South Walnut Creek drainage. Contaminated water in the
drainage uttlmately enters Pond 8-5 via Pond 84.
At the meetings In February and March 1990 between DOE and the regulatory agencies, seep SW-103
was also targeted for collection. It is located within the South Walnut Creek Drainage upstream of Pond 8-5
(Figure 4-1). The seep contains trace concentrations of CO. ( < 10 ug/ l) and concentrations of total plutonium,
americium, uranium. and several metals above ARARs. However, at the time, the physiographic features of
the seep were not discussed. Of particular note is the large area of seepage (approximately 30,000 sq. ft.) and
the location of the seep on a steep hllside. These features necessitate an elaborate drainage system for
seepage collection that would require disturbance of large areas of potentially contaminated saturated soils
which would likely result in release of significant quantities of contaminants downstream. Construction at
SW-103 would also have a negative impact on the large area of wetland present at this seep. For these
reasons, and because the ca. and dissotved inorganic constituent concentrations in the seepage are low, and
the contribution of radionuclide and metals contamination from SW-103 to the South Walnut Creek drainage
above the detention ponds Is likely to be Insignificant relative to that resulting from contaminated surface water
runoff. collection of water at this seep is no longer recommended for this 1M/IRA. Since the environmental
impacts of construction of a surface water collection system at SW-103 appears to outWeigh the benefits of
collecting and treating this seepage, consideration of collection at SW-103 is deferred until additional
hydrogeological and contaminant characterization information is gathered and assessed during conduct of the
Phase II RFI/RIFS Alluvial Wort< Plan for OU 2.
SURFACE WA~R INTER... RE...EOIAL ACTION PI.Ni
ROCI(V FL..t.TS PlANT. GOlDEN. co..ORAOO
19&;"""'t'8D \ ..,nut "18C~.mar
r.tarch , l1li1
-------
EXPLANATION
-.
o 5'N- 25
Q
INDMDUAL HAZARDOUS SUBSTANCE
SITE (IHSS)
.. .
PON)
8-5
o SURFACE WAiER UONITORING STATION
SW-103 AT A SURFACE SEEP
d'"
o SURFACE WATER t.40NITORING STATION
~-23 IN A SURFACE WATER DRAINAGE
& 1M/IRA SURFACE WATER UON/TORING
SW-59 STATION AT A SURFACE SEEP
--~.. ..
.~
.~ 1 03
. 1M/IRA SURFACE WATER t.40N/TORING
SW-61 STATION IN A SURFACE WATER DRAINAGE
A IM/IRA SURFACE WATER UONITORING
SW-60 STATION AT 1HE EXIT OF A CULVERT
- -.-
- f ~ .-- ...
~
i
.. -
I
......J
Scale: 1. = 600'
.-
0' JOO' 600'
I I I
~ IHTERVAL . 20'
-
._--------,--,-. ..
"
u.s. DEPARTMENT OF ENERGY
Rocky Flats Plant
Golden, Colorado
'..-- .:..._~
.j
--
OPERABLE UNIT NO.2
SURFACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
FIGURE 4-1
SURFACE WATER
MONITORING STATIONS
POND
C-2
-.'
-.
.w~~
-
--
.; .
March, 1991
-------
.-....---
...----_:
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,~- - - .n- 1 ,.,
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-------
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.- \- - ---'
: -- ~925.6
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---
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.~
EXPLANATION
o
, SW-S9
1M/IRA SURFACE WAlER MONITORING
STATION AT A SURFACE SEEP
1M/IRA SURFACE WAlER MONITORING
STATION IN A SURFACE WAlER DRAINAGE
.
SW-61
A
SW-60
1M/IRA SURFACE WAlER MONITORING
STATION AT Ol1TFtOW OF A CULVERT
~
i
Scale: 1- = 50'
0'
I
25'
I
SO'
I
ConIDur Int8MIJ . 2'
u.s. DEPARTMENT OF ENERGY
Rocky Flats Plant
Golden, Colorado
OPERABLE UNIT NO.2
SURFACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
FIGURE 4-2
DETAIL PLAN OF SURFACE WATER STATIONS
SW-59, SW-60, SW-61, SW-132,
SW-133
March, 1991
-------
T /t'
-+s9SO I
I x
, I
~!
~
~..
/ [1
--~i --:
i : I :
I
: ! I I
'--~ L....--.-oJ
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o
-------
Several alternatives exist for collecting the contaminated South Walnut Creek Basin surface waters
mentioned above. First and foremost Is collection of surface water by diversion at the source. This technique
...
employs existing or newly constructed diversion structures at the seep or in-stream stations to divert the
surface water into collection sumps. This method of surface water collection was agreed to by EPA, COH, and
..
DOE in the February and March 1990 meetings. This technique will be further discussed and evaluated In
Section 4.3. For comparative purposes, two other surface water collection methods are discussed below.
A ~ond method of surface water collection is by ground-water withdrawal using an upgradient well
array or french drain. This technique lowers the ground-water table and eliminates seepage. allowing
separation of contaminated ground water (seepage) from surface water runoff. e.g., at SW-59. However. the
hydrogeology at OU 2 is not adequately understood to design an effective ground-water withdrawal system.
For example, It is not known whether the seepage Is due to water originating in the Rocky Flats Alluvium and
being released to the surface through colluvium because of slope changes and/or bedrock highs. or whether
the source of the water is bedrock sandstone subcropping in this vicinity. This information is critical to the
design of an effective ground water withdrawal system. EPA alluded to the issue in their transmittal letter
(January 9. 1990) which accompanied their comments on the draft OU 2 ground-water 1M/IRA Plan, wherein
they stated". . . this OU Is difficult to address on an Interim basis due to the lack of comprehensive quality data
characterizing the nature and extent of contamination. It Is uncertain whether the most probable imminent
threat. the alluvial ground-water system, can be effectively addressed at this time." For this reason. collection
of surface water by ground-water withdrawal is eliminated as a reasonable alternative for this 1M/IRA and will
not be considered for further detaled evaluation.
A third collection alternative Is to allow the contaminated surface water to continue to flow through the
South Walnut Creek drainage into detention Pond 8-5. The contaminated South Walnut Creek 8asin surface
water. along with all other waters collected and detained in Pond 8-5 would be transferred from the Pond for
treatment. This method has three primary drawbacks. First, there is a potential threat of transferring the
surface water contaminants to ground waters within the South Walnut Creek drainage basin via infiltration.
Secondly. release of VOCs to the atmosphere will occur while the surface water is in transit to detention Pond
SURHCE WATER IIoITERlI.I REMEDIAL. ACTION Pt.AN
ROCI(Y FI.ATS "!..ANT. GO.DEN. COI..OAAOO
ev&.;' 811Mr8Q '-""""", 8K~.maI'
Matc,", 1991
-------
8-5. Finally, allowing the South Walnut Creek 8asin surface waters to mix with other waters retained in Pond
8-5 generally increases the volume eX dYute contaminated water at the RFP facUity that may require treatment.
.,.'
For these reasons, collection of South Walnut Creek Basin surface waters at detention Pond 8-5 is eliminated
as a reasonable alternative for the 1M/IRA and will not be considered for further detailed evaluation.
.
4.1.2 Surface Water Treatment Technoloaies
~sed on the objectives of the Surface Water 1M/IRA discussed In Section 3.1, Table 4-1 has been
prepared to establish the basis for conceptual design for surface water treatment. The influent constituent
concentrations listed In Table 4-1 are estimated from a flow-weighted maximum concentration model based
on the maximum constituent concentrations observed at the SW-59 and SW~1 collection points. The flow
values used to weight the maximum concentrations used in the model are the corresponding collection system
design flows (established In Section 4.3 and listed in Table 4-5). A spreadsheet Dlustrating computation of the
flow-weighted maximum concentration computation is shown in Table F-1, Appendix F. To be conservative,
the maximum constituent concentrations used In the model for SW~1 also Includes maximum observed
concentrations for the group of stations upgradient of SW~1 (i.e., SW-56, SW~, and SW-1 01). Unfortunately,
station SW-132 was only recently assigned to the au 2 surface water sampling program and concentration
data for this discharge are not avaUabie for use In the treatment system design model. As discussed in
Section 1, however. the water quality characteristics of this stream are expected to be simRar to that at SW~1.
This assumption has been used to provide a reasonable conceptual treatment system design basis in the
absence of SW-132- dat8. The design basis will be updated as SW-, 32 concentration and flow data become
available to verify the Influent concentrations computed herein.
Table F-1 shows that strict application of the flow weighted concentration model predicts vinyl chloride,
methylene chloride and acetone influent concentrations above their respective ARM values. However,
examination of the surface water data presented in Appendix B reveals that these constituents are not likely
SURFACE WATt~ INTERIM REMEOIAlAC'TIOfoI PlAN
~ '"!.AT'S ""-ANT. GOI.DEN. COLORADO
~'.-F8C._nUl'._~."'"
Marcn 199'
-------
TABLE 4-1
BASIS FOR DESIGN OF SURFACE WATER TREATMENT PLANT
~
Influent Effluent
.unb . Concentration- Reaulrementsb
~ Oraanics
1,1-Dlchloroethene pg/l 142 7
1 ,1-Dichloroethane pg/l 6 1U*
1,2-Dlchloroethene (total) pg/l 10 1U*
Chloroform I/g/l 82 1U
Carbon Tetrachloride pg/l 219 5U
T richloroethene JJQ/l 153 5U*
T etrachlorbethene I/g/l 279 1U
Dissolved Metals
Berytllum mg/l 0.0053 0.1
Manganese mg/l 0.5790 0.050
Strontium mg/l 0.8396 0.396**
Tin mg/l 0.9036 0.100
Total Metals
AluminUm~) mg/l 25.1214 0.2U
Antimonre ( b) mg/l 0.0655 0.060
Barium ~ mg/l 1.8530 1.000
~lIum e) mg/l 0.0519 0.1
Ca mium (Cd) mg/l 0.0132 0.01
Chromium (Cr) mg/l 0.1918 0.05
Cobalt (Co) mg/l 0.1232 0.050
Copper (Cu) mg/l 0.2664 0.2
Iron (Fe) mg/l 183.9643 1.000
Lead (Pb) mg/l 0.1954 0.05
Uthlum (U) mg/l 0.4100 2.500
Manganese (Mn) mg/l 3.3068 1.000
Mercury (Hg) mg/l 0.0022 0.002
Molybdenum (Mo) mg/l 0.1574 0.100
Nickel (Ni) mg/l 0.2239 0.2
Selenium (se~ mg/l 0.0070 0.01
Strontium (Sr mg/l 0.8600 0.382**
Vanadium M mg/l 0.5019 0.1
Zinc (Zn) mg/l 1.3475 2.0
*
No ARAR standard exists for this constituent; effluent requirement is TBC concentration, considered
as an 1M/IRA treatment goal.
..
No ARM or TBC standard exists for this constituent; effluent requirement Is background concentration,
considered as an 1M/IRA treatment goal.
SURF"CE w..~ INTEl'll,! REMECIAL ACTION PI.AN
ROCI(Y FI.ATS "LAHT. GOLDEN. CO-ORAOO
-o.!o.;..__,_n\Jt\_-4.mat
Marcn , 88'
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TABLE 4-1 (cont.)
BASIS FOR DESIGN OF SURFACE WATER TREATMENT PLANT
'y
Influent Effluent
.I.lDtti Concentrationa Reauirementsb
..
Dissolved Radlonuclldes
Gross Alpha pCl! I 20.11 11
Gross Beta pQI/1 39.90 19
Total Uranium pCi/1 9.96 10
Total Radionuclldes
Gross Alpha pCI/1 730 11
Gross Beta pCl/1 545 19
Plutonium 239.240 pCi/1 3.28 0.05
Americium 241 pCi/ I 0.53 0.05
Total Uranium pCl/1 11.69 10
a
The influent concentrations are based on flow-weighted maximum concentrations of station SW-59 and
the following group of stations: SW-56. SW~. SW~1. and SW-101. The computation Is Ulustrated by
the spreadsheet shown in Table F-1, Appendix F. The maximum observed concentrations for each
station or group of stations is multiplied by the corresponding collection station design flow. The
multiplication products for each collection station are summed and divided by the sum of the CS-59 and
CS-61 design flows (42 gpm). Concentration data used In the flow-weighted maximum concentration
computation Is obtained from the 1987, 1988. 1989. and 1990 field investigations.
b
Based on Applicable or Relevant and Appropriate Requirements (ARMs). The .U. designation following
many of the efftuent concentrations Indicates that the concentration is the detection limit for that
constituent.
SURFAce WA~ INTeRl... REIotEOlAL ACT10N P\.AN
I'IOO(Y FLATS PLANT. GO\.DEN. co..OAAOO
e;&g'._rac'_nUl._~.rnar
Marcn , 1191
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to be present in the influent at levels above ARAR. Vinyt chloride, methytene chloride and acetone were
detected at levels above ARAR only at stations SW-56. SW~ and SW-101. However, as proposed in
~
Section 4-3. contaminated surface water from these stations wUl be collected at the downstream station SW~1
where vinyt chloride. methytene chloride and acetone have always been estimated below detection limits
.
and/or were also present in the associated laboratory blanks. These compounds are, therefore, not included
in the basis for design of the surface water treatment plant. The effluent concentrations listed In Table 4.1
correspond to the ARAR for each constituent.
Treatment technologies for radionuclides and metals removal that are considered In this 1M/IRA Plan
include chemical precipitation, cross-flow membrane filtration, and Ion exchange. Uquid-phase Granular
Activated Carbon (GAC) adsorption, air stripping with liquid and vapor phase GAC adsorption, and ultraviolet
(UV) /peroxide oxidation are considered for VOC removal. Many treatment units suitable for removal of VOCs
and radionuclides from water require that suspended solids be removed from the influent to prevent
performance degradation and/or fouling. Removal of suspended solids down to the 1 pm particle size range
ensures optimum treatment system performance. The two candidate influent pretreatment alternatives for
removal of suspended solids considered for this 1M/IRA are cross-flow membrane filtration and polymer
addition with granular media filtration In a continuous backwash filter. Pretreatment Is also a vehicle for
removal of particulate radionuclldes and metals and. with chemical addition. should facHltate precipitation and
adsorption of soluble radionuclldes and metals.
4.2
IM/IRA ALTERNATIVE EVALUATION PROCESS
The following discussion of the 1M/IRA alternative evaluation process is based on EPA guidance set
forth in the March 1990 NCP.
SURFACE WATER IN'1'9tItl FEItIEDIAL ACTION PI.AN
I'CICKY ~l.ATS PLANT. GO..DEN. cc::I\.ORAOO
~ \ WMI8C) ,.-.nUf\eece4.mar
ItIarch '88'
-------
4.2.1
Effectiveness
The crtteria for effectiveness evaluation of remedial alternatives Includes protection and the use of
~
alternatives to land disposal. Protection includes protection of the community and workers during the remedial
action; threat reduction; length of time untU protection is achieved; compliance with criteria. advisories and
.
guidance; risk of potential exposure to residuals remaining on site; and continued reliability over the life of the
1M/IRA. The effectiveness crtterla also Includes use of alternatives to land disposal. thus promoting treatment
or recycling. In addition. the alternatives will be evaluated wtth respect to reduction of toxicity, mobility, and
volume of wastes per the March 1990 NCP.
4.2.2 Imclementabilltv
The criteria for implementabillty evaluation of remedial alternatives includes technical feasibility.
availability. and administrative feasibUIty. Technical feasibAIty Includes the abUityto: construct the technology;
maintain Its operation; meet process efficiencies or performance goals; demonstrated performance; evaluate
Impact of environmental conditions; and comply with the SARA requirement that removal actions should
contribute to the efficient performance of long-term remedial action to the extent practicable. AvaUabUIty
Includes the avalability of necessary equipment, materials and personnel; avaUabillty of adequate off-site
treatment, storage, and disposal capacity, If appropriate; and description of post-remedial site controls which
wDl be required at the completion of the action. Administrative feasibility Includes the likelihood of public
acceptance of the alternative, Including site and local concern; coordination of activities with other agencies;
and ability to obtain any necessary approvals or permits.
4.2.3 ~
The criteria for evaluation of remedial alternative cost includes total cost and statutory limits. T ota! cost
includes direct capital costs, indirect capital costs, and operating and maintenance costs. Since the surface
water 1M/IRA at au 2 is not an EPA-financed remedial action. the $2 million statutory cost limit does not apply.
SU~J.CE WA'TER I~ REMECW. AC'T1ON P\.AN
ROCI
-------
4.3
EVALUATION OF THE IM/IRA SURFACE WATER COLLECTION SYSTEM
~
As discussed eartler. South Walnut Creek Basin contaminated surface waters will be collected by
diversion at the sources. This section further describes this technique as It applies to the surface water seep
..
and In-stream monitoring stations considered in this 1M/IRA. This presentation includes a discussion of the
anticipated seep and In-stream monitoring station flows. and an evaluation of the collection technique per the
evaluation process outlined In Section 4.2.
4.3.1
Surface Water Collection bv Diversion at the Sources
4.3.1.1 Description
Figure 4-3 shows the locations of ~ surface water diversion and collection systems proposed for the
1M/IRA. The collection systems (05s) are denoted 05-59. CS~1. and CS-132. The proposed location of the
surface water treatment plant Is also Indicated on Figure 4-3. The CSs provide for automatic pipeline transfer
of the collected surface water to the treatment system.
Design flow rates for surface water collection systems CS-59. CS~1. and 05-132 are based on flows
from stations SW-59. SW~1. and SW-132. respectively. The design flow rates are maximum flows observed
in the 1988. 1989, and 1990 field investigations. excluding flows related to high precipitation events. Only
design flows wli be collected from the South Walnut Creek Basin surface water monitoring stations. Historical
flow data for SW-59 are listed In Table 4-2. Table 4-2 lists only two flow rates of sufficient quantity to be
measurable for SW-59 (each 4.5 gallons per minute [gpm)). Rocky Rats personnel have observed flows at
SW-59 monthly since Spring 1990. They report that a flow of approximately 0.5 gpm was occurring at each
observation. It Is expected that all flows at SW-59 will be diverted for treatment.
Historical flow data for SW-61 are listed in Table 4-3. Table 4-3 Indicates two high flow events for SW-
61 of 166 gpm. All other historical flow data for SW-61 are below 36 gpm. To complement the historical data
SURFACE WATeR INTC"M FlEMECIAl ACT10N PlAN
ROCI(Y ~LATS~. GOI..DEN. co..ORAOO
ev&; \ -_,--.UI'I8C.."'"
March 188'
-------
EXPLANATION
.
5W-61
1M/IRA SURFACE WA1ER MONrTORING
STAllON AT A SURFACE SEEP
It.I/IRA SURFACE WA1ER MONrTORlNG
STAllON IN A SURFACE WATER DRAINAGE
.
5W-59
o
CS-61
It.I/IRA SURFACE WATER MONITORING
STAllON AT OllTFLOW OF A CULVERT
SURFACE WATER DIVERSION AND
COw:cnON SYSTEM
---
SURFACE WATER TRANSFER PIPEUNE
TREATIAENT SYSTEM DISCHARGE PIPE
-'-
. -
~
1
Scale: 1- = 100'
0'
I
SO'
I
100'
I
CcInW IntIMII . 2'
u.s. DEPARTMENT Of ENERGY
Rocky flats Plant
Golden, Colorado
OPERABLE UNIT NO.2
SURfACE WATER 1M/IRA
SOUTH WALNUT CREEK BASIN
fiGURE 4-3 \
.- LOCATION Of PROPOSED SURfACE WATER I
COLLECTION AND TREATMENT fACILITY
~
~
-------
TABLE 4-2
SURFACE WATER FLOW DATA FOR SW-S8'
~
Row (GPM)2
Date of Row
Measurement
.
4.5
4.5
o
o
o
o
o
o
o
o
07/01/88
03/20/89
05/11/89
06/08/89
07/06/89
08/10/89
09/18/89
10/03/89
11/06/89
12/06/89
Flow data are obtained from the 1988 and 1989 field investigations.
2
A flow rate of zero indicates either no seepage or an Imperceptible flow. Rocky Rats personnel
observed flows at SW-59 monthly since the spring of 1990. They repon that a flow of approximately
0.5 gpm was occurring at each observation.
SU~ACE WA~ INTER" REMECIAL AC'T1ON F>lAN
~I(V .\.ATS F'\.AHT. GOI.DEN. COI.ORAOO
'9AG". ""11'8Q \ walnut \ 18C~.rnat
Matc~ '118'
-------
TABLE 4-3
SURFACE WATER FLOW DATA FOR SW-81'
"
Flow (GPM)2
Date of Flow
Measurement
35.9
166
9.0
9.0
9.0
4.5
18.0
4.5
4.5
o
18.0
166
07/01/88
03/20/89
05/15/89
06/09/89
07/06/89
08/03/89
09/11/89
10/03/89
11/06/89
12/06/89
02/09/90
03/12/90
..
Flow data are obtained from the 1988. 1989 and 1990 field investigations.
2
A flow rate of zero indicates either no seepage or an imperceptible flow.
SURF ACE WA'ICR INTE'lM AEMEOIAL ACTION PLAN
ROCICY FI.A TS I'UHT. GOLDEN. COI..OAAOO
.; .-._._null_04.1ft81
IoIarcn , 89'
-------
and to obtain wet season flow data not corresponding to a major precipitation event, a flow measurement at
SW~1 was obtained In April 1990. A cutthroat flume manufactured by Bask! Water Instruments, Inc. was used
~
to measure the flow at SW~1. A flow of 37.5 gpm at SW~1 was recorded.
Historical flow data are not avaUabie at SW-132 as this Is a newty designated monitoring station.
.'
However, It was observed during October 1990 and December 1990 field surveys that the flow at SW-132 was
approximatety equal to the flow at SW-«J. The design flow rate for CS-132 wil thus be based on historical flow
data for SW-«J. Table 4-4 Indicates a maximum observed flow of 18 gpm for SW-«J.
Based on the historical data avaBabie and the April 1990 field measurement, design flow rates and
average annual withdrawal rates for each of the collection systems were established. The design and
withdrawal flow rates are presented In Table 4-5. A design flow of 37.5 gpm is assigned to SW-61. This flow
represents an above-everage precipitation wet season flow not corresponding to a major storm event. The
historical maximum flow for SW-59, 4.5 gpm, is used as the design basis for the collection system at this seep.
A design flow of 18 gpm Is assigned to 0$-132 based on the historical maximum flow observed at SW~.
Average annual withdrawal rates shown in Table 4-5 are estimated as follows: For SW~1, the historical flow
data spanning the 12-month period of March 1989 to March 1990 (See Table 4-3) is averaged. In the averaging
process 37.5 gpm, the design withdrawal rate at SW-61, Is substituted for 166 gpm for the 3/20/89 and
3/12/90 recorded measurements. This calctUtlon gives an annual average withdrawal rate of approximately
14 gpm. Averaging the historical flow data for SW-59 (See Table 4-2), the annual average withdrawal rate at
SW-59 Is found to be 8PProxImately 1 gpm. As with the design flow rate for SW-132. the annual average
withdrawal rate for SW-132 wli be estimated from historical flow data at SW-«J. Averaging the historical flow
data at SW-«J gives an estimate of the annual average withdrawal rate of 5 gpm at SW-132.
SURF ACE WA 1CR 1'fTER1oI AEIoIEDIAL ACT10N PI.AN
ROCXv FLATS PI.AHT. GOoDEN. COU)IW)O
ev&Q\--\_Ul\-~.,...,
MarcI'I , 118 ,
-------
TABLE 4-4
SURFACE WATER FLOW DATA FOR SW-eo'
...
Flow lGPM)2
Date of Flow
Measurement
o
4.5
4.5
9.0
4.5
4.5
4.5
18.0
4.5
o
o
07/01/88
03/16/88
03/16/89
05/15/89
06/09/89
07/06/89
08/03/89
09/11/89
10/03/89
11/06/89
12/06/89
,1t
Flow data are obtained from the 1988 and 1989 field investigations.
2
A flow rate c:A zero indicates either no seepage or an imperceptible flow.
SURFACE WATER IHTERIooI ~ECIAL AC'T1ON PI..AN
ROCi(V FLoATS PI..ANr. GCU)EN. COLOfW)O
~'._._n,,!\_...,,*
Marc~ 1119'
-------
TABLE 4-5
....
DESIGN FLOWS AND AVERAGE ANNUAL WITHDRAWAL
RATES FOR SURFACE WATER DIVERSION AND COLLECTION SYSTEM
AVERAGE ANNUAL
..
STATION
DESIGN FlOW (GPM)
WITHDRAWAL RATES (GPM)
SW-59
4.5
1
SW~1
37.5
14
SW-132
18.0
5
TOTAL
60.0 gpm
20 gpm
SURFACe WA'TCR IHTE'M REMECW. AC'T1ON P\.AN
ROCKY FI.A 1$ PlANT. GOI.l)EN. COI..ORAOO
~"....._\~\-...",.,
Marc'" 1 ee,
-------
The flows from SW-«) and SW-133 wHI be collected at the downstream station SW~1 by a new surface
water diversion weir and pump station. A schematic of an example surface water diversion and collection
system is illustrated In Figure 4-4. The weir at SW~1 wUI serve to diven up to 37.5 gpm from the drainage.
-.-
Contaminated surface water wUI flow from upstream of the weir to a manhole and sump. For cost estimating
purposes, It will be assumed that a 1,ooo-gaJlon capacity, precast concrete sump will be used at CS~1.
Submersible pumps Installed in the sump along with a level control system wli automatically transfer collected
..
water to the treatment facUity. The pumping capacity wBl be designed to accommodate the 37.5 gpm design
flow. If the Inflow Into the pump station manhole exceeds the pumping rate, however, the excess flow will
return through overflow piping to the drainage immediatefy downstream of the CS~1 weir. The seep flow from
SW-59 Will be Isolated from the South Walnut Creek drainage and collected separately from CS~1 by
diversion into a sump. For cost estimating purposes, It is assumed that a 5OO~lon capacity,precast concrete
sump will be used. Submersible pumps and level controls will automatically transfer the collected water to the
treatment system. The pumping capacity wUI be designed to accommodate the 4.5-gpm design flow for CS-59.
Although unlikely, If the Inflow to the CS-59 pump station exceeds the pumping capacity, the excess flow will
be discharged to South Walnut Creek via an overflow pipe. The overflow wUI enter South Walnut Creek
upgradient of CS~1 and will either be collected by, or allowed to pass, CS~1 depending on whether the creek
flow Is less thein or greater than the 37.5 gpm design flow for CS~1. The flow at SW-132 will be collected and
transferred to the treatment system In the same manner as for flow at SW~1. CS-132 wUI be designed,
however, to divert and collect 18 gpm. For cost estimating purposes, a 1,OOO-galion pre-cast concrete sump
will be used.
All sumps and pipes will be provided with secondary containment to meet RCRA tank regulations.
Pipelines will be heat traced and Insulated to prevent freezing in the winter.
4.3.1.2 Effectiveness
Collection of au 2 surface water in the South Walnut Creek Basin by diversion at the sources Is an
effective method that satisfies the objectives of the 1M/IRA discussed in Section 3.1. Minimization of potential
SURFACE w.t.TER INTERIM REIoIECW..t.C'T1ON PI.AN
RXXY F~TS PlAN'T. GOLDEN. COI.OR.t.OO
~ .-_,_ftUlI_..."'"
Marcft 188'
-------
R370mJlBI22780
i~i
J~~
.. ~ ~
I~~
.- ~I
. .
';1
h
,
41
t -
-.
.. -
Drainage
---
-- I
--
--------
n ,
'(._..-..~
. . -....
_.._..~.._..
..
~
SURFACE WAlER OVERflOW WEIR DIVERTS ALl
FLOWS LESS THAN OR EQUAl TO DESIGN FLOW
TO PUMP STAllON
-------
--
--
--
--
---- --
J"" ~:-_~--
---
SURFACE WATER PUMP
STAllON INCLUDES SUMP
AND TRANSFER PUMP
---
TO TREATMENT SYSTEM
.. EQUAUZAllON TANK
NOT TO SCALE
FIGURE 4-4
TYPICAL SURFACE WATER DIVERSION AND COLLECTION SYSTEM
-------
threats to human health and the environment is achieved by diverting, collecting, and treating contaminated
surface waters at or near the source. Downstream contaminant migration via surface water and ground water
and release of VOCs to the atmosphere is minimized with this surface water collection system. The
..
implementation of this collection action should not adversely affect the safety of nearby communities, and the
risk to the environment should not be increased.
..
The surface water is collected and automatically transferred to the treatment system with little
opportunity for worker contact. As a result worker exposure to potentially contaminated surface water is
minimized. Where worker exposure to surface water occurs (i.e., sediment removal), pumping equipment
minimizes contact time, and standard personal protective equipment will offer a high degree of protection.
Residuals (Le., collected sediments) will not remain on site; they WIll be treated or disposed according
to the standard RFP waste management procedures and project-specific SOPs. The SOPs will be prepared
after the 1M/IRA design is finalized to address specific waste handling activities. The collection structures are
simple in design, and will require little periodic preventive maintenance to ensure continued reliability over the
life of the 1M/IRA.
4.3.1.3 Implementability
The equipment and materials required to construct the surface water diversion and collection systems
are standard and readily available. The systems are standard in design and do not require special skills for
installation. Sump installation may result in disturbance of potentially contaminated soils and potential impact
to the environment by release of contaminated dust to the atmosphere and release of contaminated soil via
surface water runoff. This impact will be minimized by implementing project-specific health and safety plan
procedures during construction (e.g., dust suppression, windspeed monitoring/construction shutdown). The
health and safety guidance documents pertinent to this 1M/IRA Plan are discussed in Section 7. The proposed
collection system locations are easily accessible and power exists in the area. Since the collection systems
SURFACE WA1ER II'lTERIM REMEDIAL ACTlON PlAN
ROCKY FLATS PlANT. GOlDEN, COLORADO
"9&9 \ -'rap \ waJnul\_".mar
March 1991
-------
are simple In design they should offer reliable and relatively malntenance-free operation over the life of the
1M/IRA. ManhcHs and sumps will require periodic cleaning to remove accumulated solids.
..
4.3.1.4 Costs
~"
Assumed capital and operating costs for the surface water diversion alternative are shown In Table 4~.
The collection system can be constructed for $203,500. wtth annual operatJon and maintenance costs of
$14,600. At an interest rate of 10 percent and an operating life of 30 years, the present worth of this system
is approximately $341,100.
4.4.
EVAWATION OF SURFACE WATER TREATMENT TECHNOLOGIES
4.4.1 Susoended Solids Removal
In this section, chemIcaJ treatment/cross-ftow membrane fItratIon (in this document .chemical
treatrnenr Is often dropped from .chemical tre8tment/cross-ftow membrane titration. for brevtty) and granular
media titration using a polymer and continuous backwash titer are evaluated to detennine the cost-effective
technology for suspended solids removal. These two processes differ from conventional water clarification
(chemical addition followed by gravity separation and fItratIon) by virtue of the lower sludge volumes
generated. As discUSSed In the following subsections, each of these technologies will also remove
radlonuclidea and metals to . certaJn degree.
4.4.1.1 Cross-FIow Membrane FItration
DescrlDtlon
Cross-ftow membrane filtration Is a membrane separation technology for removal of suspended solids,
diSSOlved metals. and radionuclides. (Chemical addition and removal mechanisms for dissolved metals and
SURF~ WATER IHTERM REMEDIAl AC"T1ON PLAN
FIOCI(Y"LAn! PI.AHT. Ga..OeN. ~
ee&Q"'--I-UlI_...",..
'-'arch '881
-------
TABLE 4-6
ASSUMED COSTS FOR SURFACE WATER DIVERSION
AND COLLECTION SYSTEMS
..
A.
EQUIPMENT AND MATERIALS
CAPITAL COST
(DOLLARS)
ANNUALCOST
(DOLLARS)
Quantity
2
1
6
1200 1.1.
400 cu yd
3
.!mm
1 ()()()..gallon precast concrete sump
5OO-gaIion precast concrete sump
Uquld transfer pump
Insulated heat traced piping
Concrete
Pump station Intake structures
.
4,000
1,000
3,000
4,200
50,000
3,000
INSTALLATION
QuantitY .!mm
3 1 Diversion structure
3 2 Sump installation
1 lot ' Surface water diversion berms
1 lot . Contaminated sol disposal
36,200
17,000
6,900
10,400
Inat8II8tion 008tI for 8UIt8ce WId8r dlver8ion 1trUCtur81 at C&58, CSt1, and C$-132 818 bu8d on 520 mannours of labor at
MOthr, plua . $5,000 b8dcho8 r8nt8I ctw;e.
2
Sump Inat8lIatIon 008tI818 b888cI on 200 manhourl of labor at l8O/hr, plua. $5,000 b8cIcho8 r8nt8I charg..
Surf8C8 WId8r diY8rllon b8nn 008tI 818 bu8d on eo cubic yards of fill at $11 par cubic yard, and 70 manhours of labor at S60
par hour, plua. $2.000 h8aIIy equipment r8nt8I ctw;e. A berm, 3DO feet In length, will be inatalled on NCt\ bank of the South
Walnut Cr88k dr8In8Qe. The Cf088 88CtIon of the b8rma 818 uaumed to be trapezoidal [1 toot high X 2 feet wide (top) X 3 fMt
wide (botIDm))'-
To be 00I_4iM, It 18 8ItimatIId that toils .xcavat8d for collection Iy8t8m lUmp iftlt8lJation will be di8poMd of U hazardOUI
mixed ... CI480 per oubIc yard tr8Il8pOf1ation and di8po8aI cost at the Nevada Tnt 8M). The estimated volume of .xcavat8cl
80118 Is ~ 23 cubic yards. and CCIIT8IpOnda to the following: 3 cubic yards for C&58, 10 cubic yards tor C~1, and
10 cubic y8d8 for C8-132.
~ACE WA~ ~ REMECIAL ICT'1ON FUN
ROCXY IO\.J.TS F'I.AHT.~. c::cu:IfW)O
.. ,""""'\~\8C..&.1ft8I
B.
3
.
~11181
-------
TABLE 4-6 (cont.)
ASSUMED COSTS FOR SURFACE WATER DIVERSION
AND COLLECTION SYSTEMS
. CAPITAL COSTS ANNUAL COSTS
C. OPERATION AND MAINTENANCE (DOLLARS) (DOLLARS)
Quantitv Item
.. 3 5 Collection System Cleaning $ 1,900
8 Sediment Disposal 6,000
7 Pipeline Maintenance 1,800
8 Power 2,500
SUBTOTAL $135,700 $ 12,200
D. ENGINEERING AND CONTINGENCY
Design at 25% of Capital Cost $ 33,900
Construction Management at 5% of Capital Cost 6,800
Contingency at 20% 27,100 2,400
TOTAL COST $203,500 $14,600
PRESENT WORTH
Present Worth Factor (PWF)
$14,600jyear x 9.427
1990 Capital Cost
=
9.427 (30 years, 10%i for annual costs)
$ 137,600
S 203.500
$ 341,100
=
=
Annual collection system cleaning costs are based on 32 manhours of labor at S60/hr. Collection system cleaning involves
removal of sediments that build up in the sumps and behind the diversion weirs.
8
To be conservative, it is estimated that sediments recovered from collection system cleaning will be disposed of as hazardous
mixed waste ($450 per cubic yard transportation and disposal costs at the Nevada Test Site). The cost estimated is based on
approximately 9.5 cubic yards of sediments recovered annually. This waste volume is based on an average suspended solids
concentration of 350 ppm (see Section 4.4.1.1). It is assumed that approximately 20 percent of the suspended solids in the
surface water will accumulate in the collection system sumps and trenches. and the resulting waste will be 30 percent solids by
weight.
7
Annual pipeline maintenance costs are based on 100 manhours of labor at S60/hr.
8
Annual electrical power costs are based on two 3-hp (CS-61 and CS-132) and one 1-hp (CS-59) liquid transfer pumps at
$O.07/Kwh.
SURFACE WATER INTERIM REMEDIAL ACTION PlAN
ROCKY FLATS PLANT, GOLOEN. COlORADO
eg&g\_irap'walnut'-~-mar
March 1991
-------
radionuclides are discussed In Section 4.4.2.1.) As shown In Figure 0\.5, the process consists of chemical
addition, filtration through a 0.1 I/ff1 filter, solids recirculation, solids separation and dewatering, and final
neutralization. M dl8cussed In more detai in Section 4.4.2.1, chemical addition is a pretreatment step for
f;
initiating precipitation, co-preclpltatlon, and adsorption of metals, I.e., conversion to the solid phase. However,
the solids will aid in the removal of Influent suspended solids by coagulation of fine particles and/or
enmeshment In the hydrous metal oxide ftoes. The pretreated feed combines with the recycle stream (2 to 5
."
percent solids) from the membrane filtration unit and Is subsequently filtered mechanically. The membrane filter
Is in a shell and tube configuration with the membrane on the Inside of the tubes. The permeate passes
-
through the tubes perpendicular to the main ftow at a low operating pressure. The ftux through the filter Is high
relative to other membrane technologies, e.g., reverse osmosis and ultrafiltration, because of the large pore
diameter of the titer. Flux rates of 200 to 400 gallons per square foot per day (gaI/tt2 /d) are typical for the
membrane. A fraction of the recycle slurry Is bled off for solids removal through gravity separation and
mechanical dewatering. The permeate (ftow passing through the filter) Is neutralized by addition of sutfuric acid
prior to discharge.
For the surface water 1M/IRA. It Is assumed for costing purposes that a modular and skld-mounted unit
will be required, with an assumed output capacity of 40 to eo gpm and approximately 40 kAowatts (KW) of
power. The unit would contain the following components:
. 2 12OO-ga11on reaction tanks;
- 1 ~ 0QrM:n411idon tank;
. 1 7~ recircUatJon pump
. 1 cleaning syIt8m; and
- 28 tubular membrane filtration modules.
Auxiliary tanks and process equipment would Include:
. 2 250-gallon chemical feed tanks;
SURFACE WATER INTER" REMECW. ACTION PI..AH
ROQCY F~TS PI..ANT. GOI.CIEN. COI..CFWX)
~\_\_nlll\-..-
Mare"'.'
-------
!~i
,~~
~ -I:f
j"'i
~ ~3
.. l
~;,
h
~
If
t -
tJI~
R51006.MB '-091290
"""""
CHEMICAL
. PRETREATMENT
~R[CIPrrATING AGENTS
~~PH ~ pH
,
SURFACE WATER
INFLUENT
. . . . . . . . . . . . . . .. """"""
EQUAUZATION
TANK
. ...............................
fEED EQUAUZA TlON
R£ACTION
TAN:L
R£ACTION
TAN;L
CONCENTRATION
L~K
RECIRCULATION
PUMP
. .............-.................................
""""""'" .
SETTUNG
TANK
TOA:
SOUDS TO DISPOSAL :
. ...............
. . . . . . . . . . . . . . . . . . . . . . . . . . - . . . . . . . . . . . . . . . . . . . - . .
SOLIDS DEWATERING EQUIPMENT
FIGURE 4-5
CROSS-flOW filTRATION
.
I I
I MEMBRANE MODULES I
I I
I I
I .
I I
! C~~~-~O?!_------- ----j
! ~ ~ING
I T~K TANK DRAIN TO
I STORAGE TANK OR
~-____l______l NEU~ZATION
. ......................
............... .
. ...................................
NEUTRAlIZA TlON
PROPOSED CROSS FLOW MEMBRANE FlL TRA nON SYSTEM SCHEMATIC
.
..
RECYClE
STREAM
TREATED
-------
- 1 15OO-ga11on solids sedimentation tank;
- 1 1 O~ubic-feet per day plate and frame filter press for sludge dewatering; and
..
- 1 10,00D-gaI1on feed equalization tank.
Effectiveness
.
Cross-flow membrane titration Is effective at removal of suspended solids. There are numerous
applications of this technology In use throughout the United States. Effluent suspended solids concentrations
are less than 1 mg/ I (nepe! and Shorr. 1985). Because the radionuclldes and metals are largely associated
with the suspended solid fraction (see Section 4.4.2.1). simple suspended solids removal Is anticipated to
remove greater than 99 percent of these constituents. Toxicity of contaminated surface waters is thus
significantly reduced In terms of potential future radlonuclldes and metals exposure. and It is likely that the
ARARs will be achieved with the proper chemical feed. Treated water will be monitored to ensure contaminants
are within regutatory guidelines. Cross-flow membrane filtration provides reliable and automated surface water
treatment service requiring minimal operator intervention. Workers can be easny trained on the safe operation
of the unit and handling of dewatered solids. This. together with health and safety design considerations (trailer
venting, alarm/emergency shutdown systems. automated clean-in-place equipment. etc.) provides a high
degree of worker protection. Sludges generated by the cross-flow membrane titration process wUI be handled
according to the RFP standard waste management procedures and project-specific SOPs.
I mDiernentabAItV-
Cross-flow membrane filtration as described above has been used in industry and municipalities for
wastewater treatment and for ground-water and surface water remediation since 1979. There are hundreds
of units in operation today demonstrating that cross-flow membrane fUtratlon Is a reliable process. The high
solids content of the recycle flow produces scour action on the membrane. minimizing fouling and thus the
cleaning frequency (1 hour fNery 40 to 80 hours of operation). The membrane, an inert fluorocarbon material.
can be cleaned with strong oxidants (hypochlorite) to remove bacterial films. or strong acids or bases to
SURFACe WA'TER INTCRM REMEDIAL ACT10N PI.AN
ROCI(V FL.4 TS I'\.N(T. GOU:IEN. CO\.ORAOO
e;6.;"~ ._,,,,,,_.........
Marc~ 1l1li1
-------
remove deposited metal hydroxides. The membrane will not degrade In the presence of the dUute .
concentrations of the solvents in the surface water. The equipment required to construct a cross-flow
~
membrane filtration system is standard and readily available and special skills are not required for installation.
Off-site permitted disposal facilities are available for disposal of treatment residuals.
..
The demonstrated performance and anticipated effectiveness for remediating au 2 surface waters
collected from South Walnut Creek Basin should result in a high degree of public acceptance of cross-flow
membrane filtration.
~
Assumed capital and operational costs for the cross-flow membrane filtration system are shown in
Table 4-7. Note that since the economic analysis of the treatment alternatives is a comparative one, process
stream monitoring and analysis costs are not included in the cost estimate for cross.flow membrane filtration
or other treatment units examined in this section since these costs are common to all treatment units. In
calculating sludge disposal costs, values for influent suspended solids concentration (350 ppm) and average
annual year-round influent flow (20 gpm) were estimated. The influent suspended solids concentration is
based on a flow-weighted average concentration calculation similar to that used for calculating the influent
contaminant concentrations in Table 4-1. The suspended solids concentration data used in the computation
was obtained from the 1987, 1988 and 1989 field investigations. The average year-round influent flow of
20 gpm is estimated in Section 4.3.1.1. A cross-flow membrane filtration system can be installed for $486,500.
with annual operation and maintenance costs of $249.000 per year. Assuming a 10 percent interest rate and
a 3O-year operating life, the present worth of the system is $2.833.500.
SURFACE WATER INTERIM REMEOIAl ACTION PLAN
ROCI(V FLATS PLANT, GOLDEN, COLORADO
eg&9\_i'",,\ walnut'Ioec:"'.mar
_,99,
-------
TABLE 4-7
ASSUMED COSTS FOR CROSs-FLOW MEMBRANE FILTRATION PROCESS
Capital Cost Annual Cost 'rf
.!.tmn (Dollars) (Do/lars)
A. Cross-Fiow Membrane F8tration Unit $216.100
(60 GPM Design Flow) -.
Includes:
Quantity .111m
2 12OO..ga11on Reaction Tank with
Mixer pH Controller and
Metering Pump
1 3OOO-gaIion Concentration Tank
1 7OO-gpm Recirculation Pump
Membrane Fltratlon Modules
Membrane Cleaning System
, Electrical
'Piping
B. AUXlUARY EQUIPMENT
Quantity .!WD
1 10.000-gaI1on Equalization Tank S 14,500
1 Ume Slurry System 11,400
Includes 25O-gaIion Tank, Mixer,
Recirculation Pump. Levef Control
2 Powdered Chemical System 6.000
l~ud.@S 25O-gaIIon Tank. Mixer,
Metering Pump
1 Neutralization System 19,500
Indudes 1~on Tank. Mixer,
Metering Pump pH monitor/controller
1 O-CU. Ft. Flter Press 36,000
Includes Feed Pump. Dumpster,
Air &lowdown System
2 TraBer 44.000
SURFACE WATER IHT'ERIM REMEDIAL ACT'OoI P\AH
ROCI
-------
'f
Item
C.
.
D.
TABLE 4-7 (cont.)
ASSUMED COSTS FOR CROSs-FLOW MEMBRANE FilTRATION PROCESS
Capital Cost
(Dollars)
Annual Cost
(Dollars)
OPERATING COSTS
ZOperation and Mainten8nce
~onltoring and Analysis
~ower
&Sludge Waste Disposal
I7reatment Chemicals
$131.000
24,500
32,000
20,000
$207,500
SUBTOTAL
ENGINEERING AND CONTINGENCY
$347,500
Design at 15% of Total Capital Cost
ConstructIon Management at 5% of
T otaJ CapItal Cost
$ 52,100
17,400
ContIngency at 20%
TOTAL COST
69.500
41.500
$486,500
$249,000
Present Worth:
2
3
.
5
8
Present Worth Factor (PWF) =
$249,ooo/year x 9.427 .
1990 CapItal Cost =
9.427 (30 years, 10%1 for annual costs)
$2,347,000
486.500
$2,833,500
e.etricaI and rnec::hanical88Nic8 for connec.1ion8 ... than or equal to 10 fMt III Included in thl cost of thl b88ic IyItIm.
Operation and INIint8nanoI for 1Urf8C8 W8I8r 1rI8tm8nt Is bald on one opIf81or plr shift. for thr.. Ihifla plr day at 2 houri
per shift, ....,." days per WIIk, at I8Ofhour.
Monitortng and analytical 008t8 art not Included b8cau88 they art the 88tTI8 for all treatment t8CI'Inoiogin oonsidered for the
1M/IRA.
Power 00It 88llmat8 18 b888d on a proot88 poMI' requirement of 40 tt:W. 0perat8d continuously at $0.07 /Kw-Hr. (Conversion
fac1Dr: 0.7457 1dIowaftI,/horMpower)
To be oonl8N8tM in 008t 88tlmating, It i8 888UmId that fibr pr... sludgl will be dilj)OsId of u a mixed wute ($450 plr
cubic yard tr8Mf)Ottation and dllpOlal cost at the NtYIda Teat Site). Annual production of filter cake i. baI8d on a daily
average Influent flow of 20 gpm containing approximately 350 ppm of auapend8d solid. and the cl'l8mical addition. noted
in footnot8 e. The filter cake proctuc8d 18 888UmId to be ~ aoIld. by weight with a density of 80 pound. plr cubic foot.
(Convtraion factora: 7.48 galion./cubic toot. 8.34 pounda of wa18r/gallon)
Chemical oonaumption 008ta art bu8d on an aY8f8g1 yIII~nd influent flow of 20 gpm. 0.3 pound. of iron and , pound
of lime required per '.000 gallon. of aurface water tr88t8d.
SURFACE WATER I~'" REMECIAI. ACT10N PlAN
~ =i..A'!'S PI.ANT. GO.DEH. co..oRAOO
89&; ._- ._n",\_04.....
~'IIII'
-------
4.4.1.2 Granular Media Filtration
OescrlDtIon
Y'
The continuous backwash, continuous upflow sand flter was Introduced to the United States in 1979
(Hetzer, 1987). As shown In Figure ~, polymer is Injected into the surface water, followed by rapid mixing
'.
in an IrHine static mixer. Water rises through the bed where flocculation, coagulation and floc removal occur.
Oean water overflows a weir at the top of the sand bed. As the water rises, sand moves downward through
the bed Countercurrent to this flow of water. This downward motion Is Induced by an air 11ft system In the
center of the bed (centralized pipe with air injection at the base) that draws the sand upward. Turbulent flow
is created In this air 11ft, scouring the dirt from the sand. The dirt/sand slurry spills over at the top of the alrtlft
Into a compartment with a perforated bottom and overflo.w weir. The rapidly setUlng sand separates from the
dirt in this compartment, and the clean sand is returned to the top of the sand bed. The dirty water exiting the
filter would be directed to a sedimentation tank, and the overflow from this tank sent back to the filter. The
solids from this tank will require dewatering and disposal waste management operating procedures.
Continuous upflow sand filters are typically designed based on a hydraulic loading of 4-5 gpm/tt2. For the
surface water 1M/IRA. a packaged fiberglass unit with filtration area of 12 tt2, a diameter of 4 feet, a height of
12 feet with a sand bed depth of 40 Inches (3.3 tons of sand), and requiring 0.5 to 1.5 standard cubic feet per
minute (SCFM) of air at 15 to 25 pounds per square Inch (psi) would be applicable. A 10,OOO-gallon settling
tank as well as a sludge conditioning and dewatering system will also be required.
Effectiveness
Granular rnedla filtration with polymer addition is as effective at removal of suspended solids as
conventional floccuatlon/coagulation and rapid sand filtration. Plutonium, americium, metals and, to a lesser
extent, uranium will be largely removed In this unit because plutonium and americium exist predominantly as
colloids in natural waters (Ortandinl, 1990). The unit operation equipment Is simple In design, offers operational
reliabUity, and requires no special skUls for installation. Workers can be easUy trained on the safe operation
SURFACE w...~ INTER'" I'E"'EDIAL ACTION F\AN
I'O:XY FLoATS P\AHT. GOlDEN. ~
.g ,_-'-"\II\_~,"""
ItI8rell 1 118 ,
-------
..
.
SURFACE
WATER
INFLUENT
~
!
I
i
:::I
ci
2
~
RECYCLE
STREAM
POLYMER
ADDmON
IN-UNE
MIXER
GRAVITY
SEPARATION
TANK
FILTER
CAKE
FIGURE 4-'
REJECT WASTE-
WATER AND
PARTICULATES
I
I
CONTINUOUS I
UPFlOW I
FILlER I
i
... F1 L TRA TE
~
AIR COMPRESSOR
GRANULAR MEDIA FILTRATION TREATMENT UNIT
SUR'AC£ WATER HTEI'IW ~ ACTION ~
RXXV A,J.TS FVHT. GOUJeN. c:o...oAAOO
~.- ._ur.....,-4."'"
"..,.." 188'
-------
of the unit and handling of dewatered solids. This, together with health and safety design considerations,
provides a high degree of worker protection. The effluent from this system will be suitable for subsequent
downstream treatment for dissolved radionuclide, metals and organics removal.
..
Imclementabilitv
.
Granular media filtration with polymer addition Is a demonstrated technology with regard to suspended
solids removal. Continuous upflow sand filters are particularty suitable for small water treatment plants where
operating personnel are limited. They operate continually without the need to be shut down for backwashlng
because they are self-cleaning and have no moving parts. The unit operation equipment required (i.e.,
continuous upflow filter, in-line static mixers, filter press, etc.) are standard and readily available. The upflow
filter with continuous backwash is available as a complete unit and a minimal amount of structural mounting
and piping is required to place it into service. Off-site permitted disposal facUlties are available for disposal of
treatment residuals. The demonstrated performance and anticipated effectiveness and reliability of granular
media filtration should result in acceptance of the technology by the public.
~
Relative to conventional suspended solids removal, granular media filtration with polymer addition is
cost effective in terms of both capital and operating expenses. Assumed capital and operational costs for the
continuous upflow sand filter and appurtenances are shown in Table 4-8. The system can be installed for
$167,100, with annual operation and maintenance costs of $82,700 per year. Assuming a 10 percent interest
rate and 3D-year operating life, the present worth of the system is $946,700.
SURFACE WATER INTERIM REMEDIAL ACTION PLAN
ROCIC'f FLATS PLANT, GOlDEN, COLORADO
eg&g\_irap\_nut\oec...mar
March 1991
-------
TABLE 4-8
ASSUMED COSTS FOR GRANULAR MEDIA FILTRATION
TREATMENT UNIT
'.
CaptaI
Cost Annual Cost
.I1im (Dollars) .QBi.
A. EQUIPMENT
OuantitY .!JIm
1 Continuous Upflow Sand FIlter $ 24,000
1 10,OOO-Gallon Equalization Tank 12,500
1 Air Compressor and Dryer 3,800
1 Pump and Associated PIping 500
1 10,OOO-Gallon Sedimentation Tank 12,500
1 1O-CUbic feet per day filter press 44,000
1 TraYer 22,000
"'
B.
OPERATION AND MAINTENANCE
'Operator and Maintenance
2Monltoring and Analysis
3Power
.Sludge Waste Disposal
5poIymer Consumption
SUBTOTAL
$ 43,800
$119,300
2,600
22,000
500
$ 68,900
c.
ENGINEERING AND CONTINGENCY
Design at 15% of Total Capital Cost $ 17,900
Construction Management at 5% of Total Capital Cost 6.000
ContIngency at 20% 23.900
13.800
TOTAL COST
$167,100
$ 82,700
PRESENT WORTH
Present Worth Factor (PWF) =
$82.700fyear.x 9.427 =
1990 CapItal Cost =
9.427 (30 years, 10%i for annual costs)
$779,600
167.100
$946.700
2
Operating and maint8nanC8 coati are baaed on 2 manhou,. of labor per day at S60/hour.
Monitoring and analytical coati art not included becau88 they are the same for all treatment technologi.. considered for this
1M/IRA.
8ectric power coati are baMd on a 3 hp pump and a 2 kw air compre8lOl' at $0.07 per kwh. (Conversion faC1or: 0.1457
kil0watt8/horMpower)
To be conservative in coat estimating, it ia uaumed that filter pr... aludge will be diapoa8d of as a mixed waste ($450 per cubic
yard tranaponation and diapouJ coat at the Nevada Teat Site). Annual produCtion of filter cake ia baMd on an average year-round
influent flow of 20 gpm containing approximately 350 ppm of suspended solidi. The filter cake produced is uaumed to be 30%
solidi by weight wittI a denlity of 80 Ibs. per cubic foot. Rationale for a 20 gpm average annual influent flow and an average TSS
influent concentration of 350 ppm ia presented in Section 4.4,1. (Conversion fa=,.: 1.48 gallona/cubic foot, 8.~ poundl of
water/gallon)
3
.
5
Polymer consumption costs are based on an average year-round influent flow of 20 gpm and 0.5 ppm polymer concentration.
SURFACE WATER INTERIM ""MEDIAL AC'T1C)Ioj P\.AN
RQCI(V "i.ATS PI..»l1', GOI.DEI'j. COI..OF\AOO
...,_,_._nut'._~,....,
Marcn , 118'
-------
4.4.2 Radionuclldes and Metals Removal
4.4.2.1 Cross-Fiow Membrane FIltration
,.
DescriDtion
.
The cross-flow membrane titration system (as applied to suspended solids removal) was previously
discussed in Section 4.4.1.1. In this section the chemistry and removal mechanisms for radionuclides and
metals. as applied to cross.flow membrane filtration, are discussed.
There are five oxidation states of plutonium (Pu) in aqueous solutions: Pu(III), Pu(IV), PuM. Pu(V1), and
Pu(VII). However, under the oxidizing and near-neutral conditions expected in the surface water. the Pu(lV)
oxidation state Is the most stable (Cleveland, 1979). Pu(lV) is practically insoluble under these conditions
because it readRy hydrolyzes to form Pu(OH)4(s) and. upon loss of water, to produce the thermodynamically
stable PuOz(s). This solid phase Is a colloidal polymer of neutral or positive charge. Increasing pH tends to
reduce the charge density of the polymer. and at pHs above 9 It Is presumed that the colloid becomes
negatively charged. This reduction in charge density and eventual conversion to an anionic form at pHs above
9 decreases Its adsorption affinity for soils and thus increases Its mobUIty in the soil/water environment. In
solution. PuM and Pu(V1) coexist as Ions with the Pu(lV) polymer. At a pH of 8. the dominant ionic form of
plutonium may be PuOzCO:sOH" occurring at a concentration of approximately 10.1ZM (1.5 x 10-6 pCl! 1).
However, the sclubiity c1 plutonium can be increased through complexation with humic acids.
Americium (Am) has one oxidation state in aqueous solutions: Am (III). Under oxidizing and near-
neutral conditions expected in surface water, Am (III) strongly complexes with colloidal material a~ should
exist in the particulate fraction (Orlandini. 1990).
There are four oxidation states of uranium In aqueous solutions: UQII). U(IV), UM, and U(VI) (Sorg.
1987). U(III) and UM are unstable. and U(VI) is the thermodynamically predicted oxidation state of uranium
SURFACE WA'TER INTERW REMEOIAI. AC'T1ON ~
RQCI(V 1'i..A TS PO..ANT. GOlDEN. CO!.OfWX)
¥i ...,..rao ...anlolf\88C"'.maf
Marc" , 99'
-------
under oxidizing conditions. U(VI) predominantly exists as the uranyl ion (U022+). The uranyl ion readily
.
complexes with the common anions chloride, sutfate, nitrate, and carbonate. In water with carbonate alkalinity
and a pH range of 7-10, the dominant soluble species of U(VI) are U02(COJ22- and U02(COJt. At pH
exceeding 9.5, the uranium hydroxide complex (U02MOH), + becomes predominant. Unlike plutonium,
~
uranium is signlficandy more soluble in water.
Soluble plutonium, americium, uranium and metals are removed from solution In the cross-flow
membrane filtration process by adsorption on a ferric hydroxide floc. The most effective removal of uranium
by conventional coagulation using Iron salts is at a pH greater than 9.5. This Is presumed to be due to the
predominance of the positively charged uranium hydroxide Ion In the presence of the negatively charged ferric
hydroxide (Sorg, 1987). Because the predomir\8nt form of plutonium and most metals in the surface water is
particulate, the cross-flow membrane filtration process will remove this radionuclide from the influent through
adsorption to, and enmeshment in, the ferric hydroxide.
Ferric sutfate [F~(SOJJ Is the iron salt of choice for introducing ferric Iron to the Influent stream.
Because of the hydrolysis of ferric iron, the pH drops to 2 or 3, which facDitates dissolution of the iron sail The
ferric sUfate is automatically fed in dry form to the Influent In reaction tank NO.1 (see Figure 4-5). The ferric
ion will rapidly hydrolyze at high pH (9 to 11) to form ferric hydroxide Fe(OH)3(s). Hydrated lime [Ca(OH)J
is automatically added in reaction tank No.2, and is used to raise the pH, which also improves the
compresslbllty of the ferric hydroxide sludge. In surface water treatment applications, iron and lime
consumption Is typically 0.3 Ibs and 1 Ib, respectively, per 1,000 gallons of Influent. These estimates will be
made more exact based on the bench and flefd-scale treatab81ty studies described in Section 6. An adjustment
with a pH controller wli be required prior to discharge of the permeate to maintain the effluent in a pH range
of 6 to 9.
SURFACE WATER INTE"101 REMEOW. ACTION PlAN
AOCI(V I'LA TS "LANT. GOlDE"'. COI.ORAOO
~; '. -rap \_n\lll_........,
Marc:P\ 1ar;1 .
-------
Effectiveness
.
Although limited. there is data demonstrating the removal of plutonium from water using cross-flow
membrane filtration. The only data avaUabie Is from a study performed at the RFP using a small-scale. cross-
flow membrane titration unit « 1 gpm) treating plutonium. and uraniu~ntaminated laundry wastewater.
.
Results are shown below:
Parameter
Concentration (pel/I)
Influent Effluent
Gross alpha
Gross beta
Total uranium
Plutonium
2,480
3,933
1,238
63.4
5.3
8.9
2.25
0.25
The plutonium removal efficiency indicated by these test results is greater than 99 percent. Other data
from previous test runs on laundry waste water indicated effluent plutonium concentrations less than the
detection limit (0.1 pel/I). Considering the complexing agents present in laundry water, It is possible that the
cross..ftC7tY membrane titration process can meet the MAR for plutonium of 0.05 pCi/ I. Using the percent
plutonium removal for the above reported test and the expected influent concentration of plutonium to the
treatment facUlty, the MAR wli be achieved based on theoretical calculations.
Data demonstrating removal of americium from natural waters is not available at the time of this writing.
HC7tYever, amer1clum's'StrOng affinity for particWites in natural waters suggests that americium should be
removed from South Walnut Creek Basin surface waters by cross..ftC7tY membrane filtration via the suspended
solids removal mechanisms. This observation is supported by examination of the dissolved and total
americium concentrations detected in South Walnut Creek Basin surface water samples (Appendix B).
Examination of these data reveals that there were no instances where dissolved americium concentrations
exceeded the ARAR. Total americium concentrations (i.e., dissolved plus particulate). however, exceeded the
ARAR on several occasions.
SURFACE WA~ IPITERIM FEMEOIAL ACTION I"lAN
~ "i.ATS ptJoHT. GQUJEN. CX>.OI'\ADO
89&;._'_nlll _04."",
M&n:~ 199'
-------
Because of its ubiquity in water supplies, there is considerably more Information on the removal of
uranium during water treatment.
Uranium removal efficiencies have been reported for conventional
~
coagulation/filtration water treatment, and data exist for cross-flow membrane filtration used at the RFP and
at Uranium Mill Tailings Remedial Action (UMTRA) sites. The UMTRA project is a DOE-sponsored program to
clean up low-level radioactive uranium mill tailings and associated contaminated surface water runoff In eleven
~
western states and Pennsylvania. With regard to conventional water treatment, using a dose of 10 mg/1 of
ferric sulfate as a coagulant with a pH of 10, 80 percent removal of uranium has been reported (Sorg, 1987).
Use of ferrous sulfate at doses between 20 to 25 mg/1 and at the same pH resulted in removals as high as
92 to 93 Percent. For cross-flow membrane filtration, the above-reported test at the RFP Indicates achieving
greater than 99 percent removal and meeting the ARAR for uranium (10 pCI/1). At the Canonsburg UMTRA
site, water containing 4,400 pCif 1 of total uranium was treated to achieve a total uranium concentration of less
than 1 pCi/1. Although specific data is unavailable, the cross-flow membrane filtration unit operating at the
Durango UMTRA site is achieving effluent uranium concentrations below the Colorado in-stream standards for
that area.
It would appear that cross-flow membrane filtration should be effective for removal of plutonium,
americium and uranium as well as other metals from South Walnut Creek Basin surface water. ARARs should
be achieved for plutonium, americium and uranium, although there is less data and correspondingly less
certainty on the performance of the system for plutonium and americium removal. ARARs for gross alpha and
gross beta should also be achieved. The gross alpha is largely from uranium and particulate forms of
plutonium and americium, and most of the gross beta arises from uranium 238 daughters, e.g., thorium 243
and protactinium 234. The thorium and protactinium predominantly exist in the particulate fraction and should
be removed by cross-flow membrane filtration via adsorption on iron hydroxide. Although cesium 137,
potassium 40, lead 210, and strontium 90 (which are more soluble) also contribute to gross beta activity, the
success of the current filtration operation to lower the gross beta concentration at Pond B-5 would indicate
that they are not significant contributors to the gross beta activity in South Walnut Creek. Removal of the
radionuclides should effectively reduce the potential threat to the public health and the environment. The ARAR
for TDS may not be achieved with cr9SS-fiow membrane filtration as a result of the addition of ferric sulfate and
lime to the process influent.
SURFACE WATER INTERIM REMEDIAL ACTlON PlAN
ROCKY FLATS Pl.ANT. GOlDEN. COLORADO
eg&9\ -,rap \ walnul\oec"'.mar
March 1 99 1
-------
The ARM for res is not a public health-based standard; rather, It is a secondary drinking water
standard set for aesthetic reasons. The bench and field-scale treatabDity studies will provide TDS concentration
data of treated effluent.
,
ImDlementabl1tv
.
See Section 4.4.1.1 for a discussion of the ImpiementabDIty of the cross-ftow membrane filtration
process. .
~
See Section 4.4.1.1 (Table 4-6) for a presentation of the assumed capital and operating and
maintenance costs of the cross-ftow membrane filtration process.
4.4.2.2 Ion Exchange
DescriDtlon
The ion exchange treatment system for the removal of radionuclides consists of a strong base anion
exchanger followed by a weak acid cation exchanger (Figure 4-7). These exchangers are designed for the
removal of uranium and plUtonium/americium, respectively. Both Ion exchangers have been designed
conservatively using a hydraulic loading less than 5 gpm/tt2 and a bed capacity less than 2 gpm/ff. This
translates to a 4-foot diameter column with a resin bed depth of 3 feet. The column wUI include 100 percent
freeboard. This freeboard Is necessary for resin expansion during regeneration or for backwashlng If required.
The strong base anion exchanger wUl contain 37.5 ff of Rohm and Haas IRA-402 resin or equivalent
in the chloride form. Regeneration wDl not be required because of the high affinity and capacity of the resin
SURF-'CE WATER I~ REWmAI.. ACTION PLAN
ROCICV FLATS PlANT. GOIJ)EN. ~
~ ,--.p,_nUl\_"."""
1oo\an:II1.,
-------
R51012.IdB '-081590
i~~
,~~
~iJ!
I~~
t. i
-II
h
~
if
t -
~~
INFLUENT -------
SURFACE
WATER
STRONG BASE
ANION EXCHANGER
(IRA-402 OR EQUIVALENT)
STRONG BASE
ANION EXCHANGER
(IRA-402 OR EQUIVALENT)
WEAK ACID
CA110N EXCHANGER
IRC-50 OR EQUIVAt£NT)
WEAK ACID
CATION EXCHANGER
(IRC-50 OR EQUIVALENT)
ON-LINE, STAND-BY UNITS
1iQJI.S
1. STRONG BASE ANION EXCHANGE RESIN IRA-402
IS MANUFACTURED BY ROHM AND HAAS COMPANY.
2. WEAK ACID CATION EXCHANGE RESIN IRC-50
IS MANUFACTURED BY ROHM AND HAAS COMPANY.
FIGURE 4-7
ION EXCHANGE TREATMENT SYSTEM
..
~
TREATED
-------
for uranium. The expected life of the unit is greater than 30 years at the expected Influent uranium
concentration. Although other anions will be adsorbed to the resin. the preferential adsorption of uranium over
other anions in solution will, over time. displace these anions. The spent resin wUI uttimately require
,.
solidification and disposal at the Nevada Test Site.
.
The cation exchanger will contain 37.5 ft' d Rohm and Haas IRC-SO weak acid cation exchange resin
or equivalent in the sodium form. This resin has a high affinity for high molecular weight metals. e.g., mercury.
copper. lead. and zinc. Published Information on the removal of plutonium and americium from natural waters
by Ion exchange has not been found. A cation exchange resin with a high affinity for heavy metals is most
likely to remove plutonium and americium because these constituents will predominantly exist as colloids
carrying a positive charge. The performance of Ion exchange for the removal of plutonium and americium is
unknown; however, It is noted that most of the plutonium and americium should be removed during upstrEN}m
suspended solids removal. There is Insufficient Information to determine the frequency at which the resin wDl
require regeneration. It Is assumed that. like the anion exchanger, the cation exchanger will not require
regeneration over the life d the 1M/IRA.
Effectiveness
Ion exchange has been proven to remove heavy metals and uranium from water to meet the ARARs.
whereas plutonium and americium removal using this technology Is unproven. Ion exchange has been used
to remove uranium from mine water for many years and has been studied extensively by EPA for the removal
of uranium from drinking water (Sorg, 1987). Ion exchange is commonly used for the removal of plutonium
from strong acid solutions, but no information exists on the use of ion exchange for the removal of plutonium
(or americium) present In natural waters. The absence of plutonium and americium removal efficiencies in Ion
exchange does not allow conclusions to be drawn with regard to its effectiveness in reducing the toxicity of
influent South Walnut Creek Basin surface waters. and thus, protection of human health and the environment
and public health.
SURFACE WA'TCR IIlTCRM REWEDW. AC'T1ON PI.AN
IO:XY ~l.I.TS Pl.I.Nf. GOI.!)EN. CQ.ORAOO
896Q '.-rap', _nUl \-........
a.tarcP'l 189'
-------
An Ion exchange system Is for the most part a self-contained and automated operation. Workers may
be easily trained on the safe operation of the system. There Is uncertainty as to whether the cation exchanger
"
(I.e., plutonium and americium removal) will require regeneration. This lends uncertainty as to the volume of
treatment residuals that will be generated as well as the degree of worker exposure in handling the
.
regeneration wastes. The anion exchanger will not require regeneration, as discussed eanier, as the uranium
carbonate complex wli preferentially displace major ions that wil initially load onto the resin.
ImciementabRItv
Ion exchange Is a well established technology that has demonstrated long-term reilabUIty and
performance In water treatment and after applications. The vessels, piping and pumps required to construct
a system are commercially available, off-the-sheff Items. The anion and cation exchange resins, however, are
specific to each application and, as suggested above, effective resins for plutonium and americium removal
from surface waters may not be readly avaIabie. If the weak acid cation exchanger requires regeneration (i.e.,
plutonium and americium removal), an acid regeneration system would be required, and the wastewater from
regeneration would require storage and treatment at the BuDding 374 Process Waste Treatment System
(chemical precipitation/flash evaporation). If regeneration of the cation exchange resin Is not required.
operation and maintenance requirements for the system wli be low. Effluent would be routinely monitored for
breakthrough of the radionuclldes shown in Table 4-1. The removal of suspended solids in a pretreatment step
Is required to prevent foUlng of the resin.
At th~ ~, the degree of uncenainty associated wtth plutonium and americium removal suggests the
public wli not readlyaccept Ion exchange as a preferred treatment technology. Demonstration of technical
feaslbllty through treatabDIty study testing Is necessary.
SURFAC€ WA'TCR IHT'ERI'" RaECW. ACTION PlAN
ROCXY FI..4TS PI.AHT. GO..OEN. c::o..ORADO
~'.-f8P'-"UI\-"'."""
....,.." '119'
-------
~
Assumed capital and operational cost for the Ion exchange system is shown In Table 4-9. Costs for
pretreatment of the Influent for removal of suspended solids are not considered in Table 4-9. The system can
,
be installed for 5289,900, with annual operation and maintenance costs of $45,400 per year. The operation
4
and maintenance cost assumes that regeneration of the weak acid cation exchange resin will not be required.
At an interest rate c:A 10 percent and an operating life of 30 years. the present worth of the system is $717,900.
4.4.3 Oraanlc Contaminant Removal
4.4.3.1 Activated Carbon Adsorption
DescriDtion
WIth a GAC adsorption system, the surface water will be pumped through two GAC columns in series
and operated in downflow flxed-bed mode (Figure 4-8). A second set of GAC columns will be maintained in
stock. Each carbon column Is 60 Inches In diameter and 87 Inches high, and contains 2000 pounds of carbon.
Based on a flow rate c:A 60 gpm. the hydraulic loading to each column wil be approximately 3 gpmjft. The
empty bed contad time for each column will be approximately 18 minutes. To completely udlze the carbon.
columns are arranged In series, allowing the lead column to become fully exhausted before regeneration whOe
the second (polishing) column ensures effluent quality. Periodic samples wli be taken from the effluent of each
unit. and when the lead unit effluent exceeds ARARs, the lead carbon column will be removed. the polishing
(second) column wit become the lead column, and a stock carbon unit will be put in service as the polishing
unit.
The carbon column with the exhausted carbon will then be shipped to an off-site location for
regeneration.
SUFF ACe WA TCFIIHTERlIol REMECIAI. ACT10N F'I.AN
ROCI(Y F\.A 15 PI.ANT. GO.DEN. OOI.ORAOO
.'r.-"',-""'\""~,"""
Malen '119'
-------
"
TABLE 4-1
ASSUMED COSTS FOR ION EXCHANGE
TREATMENT SYSTEM
.
.!1im
Capital Cost
(Dollars)
Annual Cost
(Dollars)
..
A.
EQUIPMENT
Quantltv
2
111m
Strong Anion/Weak Cation
Exchange Treatment System
$ 160,000
2
25OO-gallon Regeneration Waste Storage Tank
TraMer
3,000
$ 44,000
B.
OPERATION AND MAINTENANCE
'Operatlon and Maintenance
2Power
~onltoring and Sampling
SUBTOTAL
36,000
1,800
$ 207,000
37,800
C.
ENGINEERING AND CONTINGENCY
DesIgn at 15% of CapItal Cost
Construction Management at 5% of Capital Cost
Contingency at 20%
$ 31,100
10,400
41.400
7.600
TOTAL
289,900
45,400
PRESENT WORTH-
Present Worth Factor (PWF) =
$ 45.400jyear x 9.427 =
1990 CapItal Cost
9.427 (30 years, 10%1 for annual costs)
$ 428,000
289.900
$ 717,900
Operation and main18nanC8 008ta 818 bu8d on 50 manhours of labor per month at S eo,'hour.
2
Power 88tlma188 818 bu8d on two 2-hp pl'OC888 pump' opef8t8d con1Inuoualy at S 0.07 per kwh. (Conversion factor:
0.7457 kilowatta/hOrsepower) .
3
Monitoring and analytical costa are n01 included b8cau.. they are the same for all treatment technologie. considered tor
the IM/IRA.
SU~Aa: WA~ INTEFN REMEDIAL ACTION PI..AN
ROC)(Y ~TS PlANT. QOIJ)EN. COI..OIWX)
~ \.....,.p \ ....nut\ Me". "*
Mate" '98'
-------
R51011.MBpj-081590
i~~
'~Q
L;!~
t~~
- ~ ~
r I
ill
h
~
INFLUENT
WATER
vf
i :r
t ~
I
.Z
I
I
I
I
I
I
I
I
I
I
I
I
I
I
L_-- -,
lfAD
CARBON
COLUMN
POUSHING
CARBON
COLUMN
OPERATING UNITS
I
Z
I
I
I
r-----J
I
LEAD
CARBON
COLUMN
(STAND-BY)
POUSHING
CARBON
COLUMN
(STAND-BY)
ON-LINE. STAND-BY UNITS
fiGURE 4-1
CARBON ADSORPTION TREATMENT UNIT
TREATED
WATER
..
-------
Effectiveness
.
GAC adsorption systems have been shown to remove VOCs from contaminated water to levels that
comply with the ARMs. The EPA (Federal Register. Va. 52. No. 130. page 25698) has designated carbon
..
adsorption a "Best Avaiable Technology" for the removal of seven specific VOCs from drinking water which
includes common chlorinated solvents. This assumes that vinyl chloride, methylene chloride, and acetone are
not present at the proposed South Walnut Creek Basin surface water collection locations since these
compounds are not readly adsorbed from solution using activated carbon. The surface water quality data
presented In Appendix B Indicates that these compounds were detected at levels above ARARs only at stations
SW-56. SW-«> and SW-101. It is proposed, however, that surface water from these stations be collected at
the downstream station SW~1 where vinyl chloride, methylene chloride and acetone have always been
estimated below detection limits and/or were also present in the associated laboratory blanks. The absence
of these VOCs at SW~1 may be due to laboratory artifact Q.e., not actually present at the upstream stations),
dUution. and/or voladlzatlon.
The probabUlty of equipment faDure wUI be minimized in this system because of the redundancy of
having standby lead and polishing adsorption units In parallel to the operating units, each of which could treat
the design flow. Two additional stock units on site add to the system reliabDIty. Appropriate safety measures
required when moving and Installing large equipment will be complied with during installation. The operation
and maintenance of the system wli be by personnel who are trained in the handling of hazardous and
radioactive wastes. Wet activated carbon preferentially removes oxygen from the air. Therefore, any time
personnel are working In confined areas where oxygen may be depleted. appropriate sampling and work
procedures for potentially low~gen spaces will be falowed, Including all applicable federal and state
requirements.
The operators of the GAC system will not be exposed to VOc-laden carbon because the use of the
containerized and transportable carbon contactors allows removal and regeneration/replacement 01 the
exhausted carbon at a remote carbon reactivation site. Carbon wUl not be handled at the site. Transporting
SURF"'ce WATCFIIN'TCRI" "£MEOW. t.C'T1ON PlMI
~I(Y Fi..t. TS PI.ANT. GOU:)EN. COI..OI'WXI
"II&i',-18I> ._n..,,_..."""
UarCP'l1981
-------
the entire exhausted carbon column to the regeneration facUity ensures operators are protected from the
carbon. and the operators need only follow routine safety procedures which are appropriate to handling heavy
equipment.
,
The exhausted carbon Is generally regenerated through a thermal treatment process which strips the
volatile organics from the carbon. The organics are subsequenUy destroyed via incineration. During this
,.
regeneration process, a small quantity of ash may be generated which requires disposal at a landfill. Thus.
this process can be considered an alternative to land disposal since the carbon Is continuously recycled.
GAC adsorption treatment In sealed. ftxed-bed contactor vessels does not produce any waste streams
or vapor emissions. The safety of nearby communities should not be adversely affected and the risk of harm
to the environment should not be Increased. This treatment process will effectively remove many of the target
organic contaminants from the surface water. Treated water will be monitored at the effluent and also at an
intermediate point In the system to ensure contaminants are below the MAR .concentratlons before being
released to South Walnut Creek during Implementation of the process.
ImDlementabllltv
GAC adsorption Is a proven technology for reducing many VOCs from water. Testing performed by
Calgon (Rockwellintematlonal, 1988b) demonstrated that activated carbon can remove VOCs to meet ARARs.
A second carbon unit connected In series with the lead unit would serve as a polishing unit and will ensure
removal of the vOCa to these levels. The removat of suspended solids in a pretreatment step is required to
prevent fouling of the carbon. The carbon columns can be easUy shipped and readDy Installed. The system
should be ready to operate.at full capacity after initial adjustments and test runs. Carbon services that provide
rental and regeneration of carbon columns are common and offer an alternative to a capital purchase. A high
degree of public acceptance Is anticipated for GAC adsorption based on Its BDA T classification. and the
minimal generation of treatment residuals. These services are readily available and cost effective for an interim
action.
SURFACE WA'TER IPoITERM REWEDIAL AC'T1ON PI.AN
~ F-...TS FV./olT. GOI..I)EN, COLORADO
.. .-<81> _n"'.._~."'"
Maten , 98'
-------
~
,
It is estimated that the carbon usage rate wUl be 0.6 pounds per 1.000 gallons of surface water, based
on breakthrough of 1.1-DCA. This assumes that vinyt chloride, methytene chloride. and acetone are not
.
present at SW~1. Based on a maximum flow rate of 60 gpm, the annual consumption of carbon will be
approximately 20,000 pounds. The cost of a 2O.ooo-pounds-per-year carbon service Is $50.000. This includes
the rental and regeneration of 10 carbon columns. each containing 2.000 pounds of acttvated carbon. The cost
of round-trip shipping Is estimated at $3.000 per column. It is assumed that the exhausted carbon columns
will be shipped as a manifested hazardous waste.
Using the preceding infonnation. the assumed capital cost for installing a carbon adsorption system
is $70.600. and the assumed annual operating cost Is $170.300 as shown in Table 4-10. Costs for pretreatment
of the influent for removal of suspended solids are not considered In Table 4-10. Total cost (present worth)
of the GAC adsorption system based on 10 percent simple interest, a 3O-year duration of operation, and no
salvage value, Is estimated to be approximately $1.676.000.
4.4.3.2 Ultraviolet (UV) Peroxide OxIdation
DescriDtion
The UV jperaxide treatment unit, as designed by one manufacturer. consists of an 360-gallon. stainless-
steel oxidation chamber which provides for a surface water retention time range of 4 to 8 minutes at a peak
system flowrate of 60 gpm (Figure 4-9).
The oxidation chamber contains UV radiation lamps which are mounted horizontally in quartz sheaths.
A hydrogen peroxide feed system Is used to inject approximately 50 mgj t (per ppm of organic contaminants)
of a 50 percent H~2 solution into the surface water feed line. The surface water jperoxlde mixture then passes
SURF"'ce W"''TE~ IN'TE"II'" REMEDW....CT1ON ~
OQ:;I(Y ~'..A'!'S "'..AN" GO..':>EN, co..OAADO
89&; ~lt8CI ...,n~ 88(".P9\8t
M&re" 1 98 1
-------
TABLE 4-10
ASSUM.ED COSTS FOR GRANULAR ACTIVATED
CARBON TREATMENT SYSTEM
,
Item
Capital Cost
(Dollars)
Annual Cost
(Dollars)
A.
EQUIPMENT
4#
Quantltv
!tJm
Process Piping and Pump
3,000
TraUer
44,000
B.
OPERATION AND MAINTENANCE
1 Activated Carbon Service
2Shlpping
3pewer
.Operatlon and Maintenance
'GAC Analysis
S 50,000
30,000
1.800
55.600
4.500
SUBTOTAL
S 47,000
S 141,900
C.
ENGINEERING AND CONTINGENCY
Design at 25% of Total CapItal Cost S 11,800
ConstructIon Management at 5% of Total Capital Cost 2,400
Contingency at 20% 9.400
28.400
TOTAl
S 70.600
S 170.300
PRESENT WORTH
Present Worth~ Fader (PWF) =
S 170.300/year x 9.427 =
1990 CapItal Cost -
9~427 (30 years, 10%1 for annual costs)
S 1.605,400
70.600
S 1,676.000
Annual GAC I8IYic8 C08tI art bU8d on rental and regen.ration of ten 2.()()().pound camon column. at $ 5.000 plr column.
2
Shipping coats .. bU8d on 10 round trip column Ihipmtnta per yur at $3.000 per round-trip lhipmen1.
3
Power C08t8 .. bU8d on on. 4-hp pump @ $0.07 {kwh. (Conwr.lon factor: 0.7457 kllowattI/horMpower)
.
Operation and maint8nance C08t8 bU8d on 77 man hours of labor plr month @ seo,'hour.
5
Annual GAC analysis coats for radioactivity testing are bU8d on analysis before and aft.r .ach unit i. in _Mce at $225 per
analylil.
SURFACE W"''IER ~ REMECW. ACTION PlAN
~ ~LATS PI.N(T. GOoDE... COLOfWX)
~ .__,_r""'.""~,"'"
Mate" 1l1li1
-------
..
...
INFLUENT WATER
H-202 FEED
-------
-------
UY OXIDATION
CHAMBER
fiGURE 4-1
UV /PEROXIDE SYSTEM
SURFACE WATER IHTEMoI RBoIECW. ACnON PI.AH
~ ~LATS ~. CKIU:EN. CCl.OfWX)
89&;'--_1_.-
TREATED
WATER
R37024.1118-052380
""""'1l1li'
-------
through an in-line static mixer before entering the bottom of the oxidation chamber. The water then flows
through the reaction chamber, passing the UV lamps, before it exits the top of the oxidation chamber.
"
Effectiveness
..
The UV jperoxide system is capable of removing VOCs from the surface water to levels below the
ARARs. A technology evaluation of a demonstration unit was conducted by the EPA's Risk Reduction
Laboratory in Cincinnati, Ohio (EPA, 1990a). Ground-water treatment experiments were performed In which
residence time, ozone and hydrogen peroxide dosages, radiation intensity and influent pH were altered to
evaluate the technology. The demonstration unit achieved VOC removals greater than 90 percent. These
results indicate that the UV jperoxide treatment process is likely capable of achieving the effluent criteria for
all of the volatile organics listed in Table 4-1. However, the volatile organics may not be completely oxidized
to carbon dioxide, water, and chloride, and unintended organic degradation products may be produced.
The system requires periodic UV lamp replacement and routine maintenance, and with such
maintenance, the unit expected to have long-term reliability. The risk of failure of the system at any time is
highly unlikely. However, because surface water is expected to have widely varying concentrations of
organics,it will be difficult to ensure adequate peroxide dosage for complete organic destruction and to prevent
the appearance of excess peroxide in the effluent. While the presence of ferrous iron and manganese can
impede the effectiveness of the UV jperoxide treatment system due to the precipitation of these metals, a
manufacturer has indicated that this will not be a problem at the iron and manganese concentrations expected.
However, should precipitation problems arise, appropriate pre-treatment and post-treatment will be
implemented to correct this problem.
The UV jperoxide oxidation system will destroy VOCs present in contaminated South Walnut Creek
Basin surface water and thus represents an alternative to land disposal. The system Itself will not produce
treatment residuals. Some support unit operations (i.e., pre-treatment) for the UV jperoxide oxidation system,
however, may require residual waste management.
SURFACE WATER INTERIM REMEDIAl ACTION PlAN
ROCKY FLATS PlANT. GOlDEN, COLORADO
"9&9 \_irap \ walnut\ see-4.mar
Match '99'
-------
During operIItIon of the UV /peroxide oxidation treatment unit, the use of hydrogen peroxide. a strong
oxidizer, wli require that operators be aware of this potential hazard. The H202 bulk storage tank will be
~
property vented to assure no pressure buDdup and minimize handling exposure. Existing DOE and EG&G
health and safety guidelines at the RFP and project-specific SOPs regarding operator safety whUe working with
..-
strong oxidizers wli be foflowed. UV lamps operate utilizing high vottage, and thus caution must be used when
working with the system and during the periodic replacement of the UV lamps.
The safety of nearby communities should not be adversely affected, and the risk of harm to the
environment shoUd not be increased as this treatment process wit effectively destroy the contaminants.
Treated water wII be monitored to ensure contaminants are within regulatory gUidelines before being released
to the environment.
imDlementabBltv
UV /peroxide oxidation Is a technology for the complete destruction and detoxification of hazardous
organic compounds in aqueous solutions. Although the technology is relatively new and has had limited
application in the field, SARA requires EPA to prefer remedial actions that significantly and permanently reduce
the toxicity. mobIlty, or volume d hazardous wastes by employing innovative technologies that result in the
destruction or detoxification d the wastes. The equipment necessary to construct a UV Peroxide system is
not "off-the-sheIt', but must be designed for each individual application. The equipment components and
materials necessary to construct a system are readDy available, however.
Demonstrated performance of the UV /peroxlde ground-water treatment system has been somewhat
limited due to the relatively new development of the process. However, there are six UV /peroxlde units
currently operational or orHine and ready for operation. One of these units is located at Rocketdyne's
Santa Susana facUlty in southern California. POot-scale operations were performed on ground water containing
VOCs (TCA, TCE. etc.) at system flow rates of approximately 20 to 40 gpm. Results from the pilot scale testing
were favorable, and a UV /peroxide ground-water treatment unit has been purchased, set up, and site tested.
SURF ACE W A '!1:R IHT'ERIoI REMEOIAi. ACTION P\.AN
~I(Y -LATS Pt.»IT, GOIJ)EJoj, COlORADO
.S;'.""If8C' -..n\J'l'.88C~.rnar
~'99'
-------
Another UV jperoxlde ground-water treatment system, located locally, was visited and appeared to be a low-
maintenance, highly effective ground-water treatment unit. This system was treating ground water with TCA
.
concentrations significantly lower than those found at the 881 HUlside (approximately 7 ppb). However, the
same UV treatment process had Initially and effectively treated ground water with much higher concentrations.
....
Operating and maintenance requirements for the UV jperoxide treatment system are relatively minor.
The system wli require up to 500 kW of power, a high electrical power consumption requir~nt relative to
other treatment processes, and 12,200 poundsjyear of 50 percent ~02 solution for normal operation. Routine
maintenance of the equipment Is required and the UV lamps wli require replacement approximately fNery six
months. All four system UV lamps can be exchanged In about an hour. Influent pretreatment for suspended
solids removal Is required to prevent fouling of the oxidation chamber. Also, Influent pre- and post-treatment
for removal of Iron and manganese may be necessary as discussed above. The system wUl require careJul
observation to ensUre the system Is operating property, although system alarms will notify operators If a
problem does occur.
Public acceptance of UV jperoxlde oxidation should be favorable based on removal efficiencies
observed to date. The attribute of mineralizing VOCs present in surface water ~.e., converting them to carbon
dioxide and water) shoUd also receive a favorable response. TreatabUlty testing on contaminated South
Walnut Creek Basin surface water may be necessary to win public approval since It Is stOI a relatively new
technology.
~
Assumed costs for the UV jperoxlde ground-water treatment unit are shown in Table 4-11. Costs for
pre- and post-treatment of the influent for reasons discussed above are not considered In Table 4-11. The
capital cost for the UV jperoxide surface water treatment system is approximately $672,800. Operational costs
are $214,600 per year and include procurement of hydrogen peroxide, power utUization, labor, and lamp
suRF ACE WATER 1N'TE'I1oI REMEOIAI. AC'!1ON PIAN
q:)O(V ~I.A TS F>..ANT. GOLDEN. CC)LOAAOO
~. -rat> _nU!'-~.mar
~n '881
-------
~
A.
--
Quantity
1
2
B.
C.
TABLE 4-11
ASSUMED COSTS FOR UV PEROXIDE OXIDATION
TREATMENT SYSTEM
Capital Cost
(Dollars)
EQUIPMENT
Item
. UV Peroxide Oxidation Treatment Unit
420.000
TraU'ers
44,000
OPERATING AND MAINTENANCE COSTS'
2Hydrogen Peroxide
3Power
4Lamp Replacement
50peration and Maintenance
SUBTOTAL
464.000
ENGINEERING AND CONTINGENCY
Design at 20% of Total Capital Cost 92,800
Construction Management at 5% of Total Capital Cost 23,200
Contingency at 20% 92.800
TOTAL
672.800
PRESENT WORTH
2
3
4
5
Present Worth Factor (PWF) =
$214.600/year x 9.427 =
1990 Capital Cost =
9.427 (30 years. 10%i for annual costs)
$2.022.700
672.800
$2.695.500
Operating costs based upon a flowrate of 50 gpm. 8 hr/d.
$O.52/lb x 12.200 Ib/yr
.500 t<:W 8 hr/d @ $O.07/t<:Wh
2 times/year
85 hours per month @ $SO/hour
SURFACE WATER INTERIM REMEDIAL ACTION PLAN
ROCI(V FLATS PLANT, GOlDEN, COlORADO
eg&g\M-if8l>\ -.lnUl\I8C".m&r
Annual Cost
(Dollars)
6,400
1 02,200
9.000
61.200
178.800
35.800
214.600
March 1991
-------
replacement. Operational costs are based on a system flow rate of 60 gpm, 24 hours per day. Assuming a
10 percent Interest rate and a 30 year operating life, the present worth of the system Is $2,695,500.
~
4.4.3.3 Air Stripping with Off-Gas Treatment
'"
OescriDtlon
O~ring air stripping, VOCs are transferred from.the water to a continuously flowing airstream which is
in direct contact with the water (Figure 4-10). Influent contaminated surface water wll enter the top of a 32-
inch diameter, 34-foot air stripping column and subsequenUy contact clean air supplied through the bottom
of the column (column sizes are approximate). Appropriate air-to-water flow rates WIll be utRlzed to provide
for the optimum (99 + percent) transfer of the contaminants from the surface water to the air stream. The
treated surface water will then be pumped through a 2000-pound liquid phase carbon treatment polishing unit
(identical to the one described In Section 4.4.3.1). The air stripper emissions wUI be heated above dew point
and then passed through a vapor phase carbon system to remove the organics before being released to the
environment. The vapor Phase carbon unit will contain 2,000 pounds of carbon.
Effectiveness
The use of an air stripper Is a highly effective method of removing hazardous VOCs from water. The
efficiency of . the proceSs Is well documented. The Environmental Protection Agency (Federal Register,
Vol. 52, NO.1 30, page 25698) has designated packed tower aeration along with granular activated carbon, as
a BOAT for the removal of VOCs from drinking water.
An air stripper coupled with IIquld- and vapor-phase carbon adsorption Is a proven system that has a
dependable record of use. It is expected that this treatment process, with proper maintenance, wUI provide
the desired level of contaminant removal to meet the ARARs.
SuRFACE WATER INTERIM REMeDIAl.. AC'T1ON PI.AN
'IOCI(Y FI..ATS PI.»IT. GOlDEN. COlOl'WX)
.;..__.._n"'\88C~.....,
Marc" '119'
-------
....
INFLUENT
WATER
AIR PREHEATER
..
TREATED AIR
TO ATMOSPHERE
AIR
TRIPPING
TOWER
VAPOR PHASE CARBON
ADSORPTION SYSTEM
TREATED
WATER
AIR BLOWER
LIQUID PHASE
CARBON ADSORPTION
SYSTEM
FIGURE 4-18
AIR STRIPPING. WITH VAPOR PHASE
AND LIQUID PHASE CARBON ADSORPTION
SURFACE WAl'EFI ~ RBoIECIAL ~ PIN;
. ~ ~1..t.TS "I.AHT, QOU:JEN. c::o...oAADO
eg&; ,-- ,-"\11'.,-"."""
RJ7Q2.U1B-052380
Ma/crI 1881
-------
The system is sized for the intended maximum flow of 60 gpm and includes two vapor-phase carbon
units - one Installed and one stock. The on-site stock unit adds to system reliability. All appropriate safety
measures required when moving and Installing large equipment will be complied with during Installation. The
'"
operation and maintenance of the system wUI be performed by personnel property trained in the handling of
hazardous and radioactive wastes. Wet activated carbon preferentially removes oxygen from the air.
""
Therefore, any time personnel are working in confined areas where oxygen may be depleted, appropriate
sampling and work procedures for potentially low-oxygen spaces wUI be followed. including all applicable
federal ao9 state requirements.
The operators of the system wUI not be exposed to VOc-laden carbon from the vapor-phase or liquid-
phase carbon units because the use of containerized and transportable carbon contactors allows removal and
regeneration/replacement of the exhausted carbon at a remote carbon reactivation site. Carbon wUI not be
handled at the site. Transporting the entire exhausted carbon column itself to the regeneration facUity ensures
operators are protected from the carbon Itself and need only follow routine safety procedures when handling
heavy equipment.
The exhausted carbon Is generally regenerated through a thermal treatment process which strips the
VOCs from the carbon. The organics are subsequently destroyed via incineration. During this regeneration
process. a small quantity of ash may be generated which requires disposal at a landfill. Thus. this process can
be considered an alternative to land disposal since the carbon is continuously recycled. However, if the spent
liquid-phase carbon is determined to be a mixed waste. then it would require land disposal at a facility
permitted to accept mixed wastes. The vapor-phase carbon adsorption system will remove the organics from
the air stripper emissions before being released to the environment. Therefore. the vapor-phase carbon
adsorption system will eliminate the impact of any air stripper emissions on the public health. The safety of
nearby communities should not be adversely affected and the risk of harm to the environment should not be
increased. Treated water and air will be monitored to ensure that contaminant levels are below ARARs.
SU~ACE W-.TER INTERlt.I REMEDW. -'CT1ON ~
I'IOO
-------
ImDlementabilitv
..
The air stripper wil remove greater than 99 percent of the contaminants in the surface water. Because
the air stripper performance Is sensitive to changes in flow and contaminant concentrations, a liquid-phase
...
carbon adsorption unit Is in series with the air stripper to enhance system performance and to ensure that the
treated effluent meets MARs for VOCS. Based on a ftow rate of 60 gpm, 24 hours per day, liquid phase
carbon usage wil be approximately 11 pounds/day, and each 2OOO-pound carbon unit will require replacement
approximately fNery sbc months. Vapor phase carbon usage will be approximately 10 pounds/day, and each
2000-pound carbon unit will require replacement approximately fNery six months.
Operation of the treatment process Is relatively simple, requiring occasional cleaning of the air stripping
column and replacement of carbon. The air stripper will require cleaning to remove scale buUdup on t~e
packing material In order to maintain optimum removal efficiency. Effluent from the cleaning operation Will
require treatment in the BuDding 374 Process Waste Treatment System. The removal of suspended solids in
a pretreatment step Is required to prfNent fouling of the carbon and liquid phase adsorber. Transportation and
regeneration of the Ilquld-phase and vapor-phase carbon units at a remote carbon reactivation site wUl be
required. The air stripping with off-gas treatment system for remediating VOC-contaminated surface water is
avalable commercially and could be implemented quicldy. No difficulties are anticipated during the installation
and startup of this treatment system.
Air stripping with liquid and vapor-phase GAC adsorption should receive a high degree of public
acceptance due to Its proven track record and classification as a BOAT.
~
Assumed costs for the air stripping ground-water treatment system are shown in Table 4-12. Costs for
pretreatment of the Influent for removal of suspended solids are not considered In Table 4-12. The total capital
cost for the system Is $114,800. Operational costs are approximately $139,900 and include the cost of carbon
SURFACE WATER INTERIM REIoIECIAL ACTION PI.AN
I'O:XY .t.ATS PI.NlT. GO.DEN. COlORADO
~'._- ._nU!\88C"'.mar
_'119'
-------
TABLE 4-12
ASSUMED COSTS FOR AIR STRIPPING WITH
VAPOR AND UQUID PHASE GRANULAR ACTIVATED CARBON
Capital Cost Annual Cost 'II
Item (Dollars) (Dollars)
A. EQUIPMENT
A
Quantitv Item
Air Stripper Column 35,000
2 Trailer 44,000
Preheater 3,000
B. OPERATING AND MAINTENANCE COSTS'
2GAC Service 38,100
3Shipping 15,000
4Power 1,200
50peration and Maintenance 61,200
8GAC Analysis 1.100
SUBTOTAL $82,000 $116,600
C.
ENGINEERING AND CONTINGENCY
Design at 15% of Total Capital Cost
Construction Management at 5% of Total Capital Cost
Contingency at 20%
12,300
4,100
16.400
23.300
TOTAL
114,800
139,900
PRESENT WORTH
Present Worth Factor (PWF) =
$139,9OO/year x 9.427 =
1990 Capital Cost =
9.427 (30 years, 10%i for annual costs)
$1,318,800
114.800
$1,433,600
, Operating costs based upon a flowrate of 60 gpm, 8 hr/d.
2 Activated carbon service costs are based on rental and regeneration of five 2,ooo-pound columns at $7,600 per column
3 Shipping costs are based on 5 round-trip column shipments per year @ $3,000 per round-trip shipment
4 8 hp, 8 hr/d @ $O.07/KWh. (Conversion factor: 0.7457 kilowatts/horsepower)
5 85 hours per month @ $SO/hour
8 Annual GAC analysis costs for radioactivity testing are based on analysis before and after each liquid- and vapor-phase unit is in
service at $225 per analysis.
SURFACE WATER INTERIM REMEDIAL ACTION PlAN
AOCI
-------
column rental and regeneration. and carbon column shipments to and from the vendor. The carbon column
rental and regeneration service described in Section 4.4.3.1 will be used for both the liquid- and vapor-phase
:,.
units. It should be noted that the cost of the carbon service is based on regeneration of the carbon as a
hazardous waste. Assuming a 10 percent interest rate, a 30 year operating life. and no salvage value, the
present worth of the system Is $1.433.600.
The total present worth cost of the system based on 10 percent simple interest, a 3O-year period of
operation, and no salvage is estimated to be approximately $1,421,400. These costs do not Include any capital
or operating costs for the BuDding 374 Process Waste Treatment System associated with the treatment of the
air stripper cleaning effluent.
s.JRFACE WA~R IPlTER!M ~ AC'T1ON PlAN
~ "\.ATS P'JJ(T, GO..OEN, COLORADO
.; .~rac\'fII8In""\88C~.mar
Marcf'\ 1891
-------
-------
SECTION 5
COMPARATIVE ANALYSIS
,
..
5.1
INTRODUCTION
This section summarizes the evaluated surface water collection and treatment technologies, and
presents a tabular comparison of the evaluation resutts (Table 5-1). A recommendation is made for a preferred
surface water 1M/IRA using the comparative analysis.
5.2
COMPARISON OF TECHNOLOGIES
Collection of surface water by diversion at the sources was established in Section 4 as the only
reasonable alternative for collection of contaminated South Walnut Creek Basin surface waters in au 2 and
is. therefore. the preferred collection technique for the 1M/IRA. On the other hand. several technologies for
surface water treatment were considered.
These technologies include chemical treatment/cross-flow
membrane filtration ("cross-flow membrane filtration' is used for brevity) and granular media filtration with
polymer addition for suspended solids removal: cross-ftow membrane fUtration and ion exchange for
radionucllde and metals removal; and GAC, UV /peroxlde oxidation and air stripping with liquid- and vapor-
phase GAC for vac removal.
The cross-ftCM' membrane titration technology is the preferred method for removal of radionuclides and
metals because It Is the most likely treatment technology that wUl remove these constituents from the South
Walnut Creek BasIn surface water and generate an effluent that Is protective of public health and the
environment. This is a result of adsorption of radlonuclides and metals on a ferric hydroxide floc as described
in Section 4.4.2. It is noted that cross-ftow membrane filtration and granular media filtration with polymer
addition are both effective technologies for removal of suspended solids. However. because cross-flow
membrane filtration Is the preferred technology for radionuclide and metal removal. additional surface water
SURFACE W"TER INTeRIM AEMEOW. "CT1ON PI.AN
~ Fl..'TS F'lAN'T, GO.DEN. COLOAAOO
ovA;" --, _nlll', _.~.....,
Marc~ '99'
-------
i~;
J ~~
- ~i
!~~
1"1
~h
I~
~
"f
.; ~
:r.1!
Technotogles end
Ass~
Present Worth
Surface Vater Cottectlon
1.
cottectlon at Sources
$341,100
Suspended Sot Ids ReIIIOvat
1.
Cross-Ftow Meabrene
Fittratlon
$2,833,500
2.
Grandutar Media Flttratlon
$946,700
Radlonuctlde and Metats Removat
1.
Cross-Ftow MeRDrane
Fit trat Ion
$2,833,500
h-..---'UII6 , ..
TABLE 5-'
~MATIVE MAlYSIS OF 'E~OIOIES
Effectiveness
cbttectlon at tha source witt
.Inl.lzedollngradlentcont..lnent
transport which otherwl.e ..y
contribute to cont..lnetlon of
retention Panda 8-5 and C-2.
High ftow events wi t l transport
dilute concentrations of
cont..1 nents downgradl ent .
Shoutd reduce TSS to tess than 1
IIIll .
Proven technotogy.
lIkety to lINt ARAR for U and
evidence .uggest. ARAR for Pu
wltl atso be ..t.
Shoutd reduce TSS to tess than 1
IIIII/t.
Proven technology.
see above
IMPt.-entabltlty
using
Ea.1 ty constructed
conventlONit equl~t.
Worker and pubtlc heatth and
.afety -t be ensured through
....Itorlng and cUlt controt
..a.ures cLlrlng construction.
Rellsbte based on perfor-.:e at
other Instattatlons. Readlty
avaltsbte and .kld IIOUI'Ited for
easy Instat tatton. Sot Ids _t
be re80Ved fr08 backwash lISter.
Reasonabty sl~te o&M.
5... as for cross-ftow 8embrane
flttratton.
see above
CCJaIIents
Effectiveness outweigh.
dlfflcuttles In I~t.-entatlon.
At.o relllOve. dlssotved heavy
..tats and radlonuct Ides.
less tt ket y to llll!et ARARs, no
benefit derived for retllDvat of
dl.sotved radlonuc:ttdes and
..tats.
see above
\.
-------
i ~~
I ~~
-~i
!~~
. - I
S~~
U
~
of
oX ~
. -
~~
'AIlE 5-1 (cont.)
alFAlAIlVE AIIAL'SIS Of n-=-'OGIES
Technologies and
Ass~
Present Worth
Effect I veness
Llkety to ~t ARAR for U;
however, Meeting ARAR for Pu Is
uhcertaln.
2.
Ion EIIchange
1717,900
Orgenlc Cont_lnent ReIIIOvat
,.
Activated Carbon
11,676,000
Will ...t ARARs for orlanlcs
provided Nthylene chloride,
acetone, end vinyl chloride are
not 8bove ARAR.
2.
Air Stripping
11,433,600
Will ...t ARARs for orgenlcs
provided acetone Is not ebove
ARAR. Methylene chloride end
vinyl chloride, If present, are
wore readity adsorbed on off-gas
cerbon than I iquld-phase carbon.
Wilt not retllOve setlli-volatlles or
hlghty water solubte organics
(acetone, butenone).
3.
UV/Peroxlde
12,695,500
Should meet ARARs
Identified organics.
for
all
80&8'."" ..,8p\,....,,,..II\lb8. I IIn
IMDl~tabillty
Conventlonat technotogy, readily
avall8ble, and easily Installed.
If regeneration Is required,
aecondery waste generation with
Increased operational cOMplexity
and cost.
Conventional technology, readily
avall8ble, and easily Installed.
Upetre- radlonucllde retllOval
will allow regeneration of carbon
In lieu of disposal as a .Ixed
weste.
Effective for varl8bte ftow end
orgenlc loading.
Conventional technology, readily
avall8bte, but Installat Ion end
operation MOre cOMptex then
liquid-phase activated carbon.
Off-gas carbon wltl be necessary
to ell.lnate transfer of
cont_lnents to the atlllOsphere.
D--tre- liquid-phase cerbon
necessary to achieve COlllpt lence
with ARARs for orgenlcs beceuse
of variable organic loading.
Readily available off-the.shelf
units. Less proven technotogy
then air stripping or activated
cerbone Effective operation ..y
be difficult with varlabte
organic toedlng. More costty
than air stripping or activated
cerbone
.
.
C-.,ts
Upetre. suspended sot Ids relllOvat
necessary which ...y relllOve Pu to
achieve ARAR.
Wltl r-.ove heavy Ntats.
Data suggest vinyl chloride,
Nthytene chtorlde, end acetone
wll t not be present above ARAR.
Operationally MOre cOlllptex then
t lquld-phase cerbone Data
suggest acetone unllkety to be
present above ARAR.
Technotogy of choice for Operable
Unit Mo. 11M/IRA; however,
Inftuent flow and organic
concentration shoutd be
relatively constant for that
-------
pretreatment for suspended solids removal is not required. Granular media filtration with polymer addition is
thus eliminated from consideration In the 1M/IRA. At this time, ion exchange cannot be considered a reliable
technology for the removal d plutonium and americium because there is no supporting data on its removal
~
efficiency. Moreover, plutonium and americium will likely be colloidal in nature and less apt to readily exchange
with ions on the resin surface. The cross-flow membrane fHtratlon system Is also reliable, readily procurable.
..
and easUy installed.
~C is the treatment technology of choice for removal of VOCs. GAC is a proven technology that is
reliable, easy to operate, and the most cost effective of the three technologies examined. This technology is
not suitable for removal of vinyl chloride, methylene chloride, or acetone. However. as discussed in Section
4, these constituents are not expected, in the Influent to the treatment system, above their respective ARAR
levels. In the event that the field-scale treatabHity study indicates that vinyl chloride, methylene chlorid~ or
acetone are present at concentration levels not appropriate for liquid-phase GAC adsorption, modifications to
or replacement d the liquid-phase GAC system will be considered at that time. Although UV /peroxide can
oxidiZe all of these contaminants. effective operation is likely to be difficult with changing organic loadings from
a surface water system Q.e., process control). In addition, UV /peroxlde Is substantially more costly to install
and operate than the other organic removal technologies. Air stripping is a viable VOC treatment technology
for the South Walnut Creek Basin Surface Water 1M/IRA This process, however. is much more complex by
design than liquid-phase GAC, which makes it more difficult to operate and has a higher probability of system
downtime. Finally, the cost of air stripping with liquid and vapor-phase adsorption is roughly equal to that for
IIquid-phase GAC.
Radionudldes and metals wUI be removed upstream of the GAC unit. The GAC should. therefore. not
become a mixed waste and will be suitable for regeneration at any facUity that accepts spent carbon for
regeneration. This will provide for the ultimate destruction of the contaminants consistent with guidance in the
NCP. which requires consideration of remedial alternatives that include an alternative that removes or destroys
hazardous substances.
SURF~ WA~ IN'TERIM REMEOIAL ACT10N Pl.AN
o:ocxv Fi.A TS "I..»I'r. GOLDEN. COLOI'.AOO
~.._I- ._nUl._~."'"
~arc:1": '991
0:;89- ~4
-------
-------
SECTION 6
PROPOSED 1M/IRA
6.1
SUMMARY
The preferred South Walnut Creek Basin Surface Water 1M/IRA consists of the following components:
.1.
Surface water collection by diversion at the sources; and
2.
Treatment of surface water by chemical treatment/cross-flow membrane filtration ("cross-flow
membrane filtration" is used for brevity) followed by liquid-phase GAC treatment.
6.1.1
Surface Water Collection
Figure 4-3 shows the locations of the surface water diversion and collection systems proposed in this
alternative. The collection systems are denoted CS-59. CS~1, and CS-132. Collected surface water is
automatically transferred to the treatment system by pipeline.
Flows at stations SW-56, SW-«>, SW-101, and SW-133 will be collected at the downsteam station SW-
61 by a new surface water diversion weir and pump station. The weir will serve to divert up to 37.5 gpm (14
gpm average annual withdrawal rate) from the drainage. Contaminated surface water will be diverted upstream
of the weir into a 1 LOOO:-gaJlon precast concrete sump provided with a screen, where large debris is separated
from the flow. This screen wil require manual cleaning to remove debris. Water will be pumped from the
manhole to the treatment facUlty. When the Inflow into the sump exceeds the pumping rate. the excess flow
wUl return through overflow piping to the drainage below the weir.
The seep flow from SW-59 will be Isolated from the South Walnut Creek drainage and collected
separately from CS~1 using a SOO-gaJlon. precast concrete sump. The sump and installed pump will be
designed to collect and transfer the design flow of 4.5 gpm (1 gpm average annual withdrawal rate). Flows
SURFACE WATER INTERIM RENECIAl AC'T1ON PI.AN
ROCI
-------
in excess of 4.5 gpm wm be discharged to South Walnut Creek, via an overflow pipe, to the drainage. The
overflow will enter South Walnut Creek upgradient of CS~1 and wUl either be collected by or allowed to pass
CS~1, depending on whether the creek flow is less than or greater than the 37.5 gpm design flow for CS-61.
Upper South Walnut Creek flow wli be collected at SW-132 by a new surface water diversion weir and pump
,,'
station. The weir wli serve to divert up to 18 gpm (5 gpm average annual withdrawal rate) from the drainage.
.
Contaminated water will be diverted into a 1000-gallon precast concrete sump. Flow in excess of the design
flow (18 gpm) will be permitted to overflow the diversion weir.
The design flow and annual average withdrawal rates for the South Walnut Creek drainage (i.e., CS-59.
CS~1, and C5-132) are 60 gpm and 20 gpm, respectively. It is proposed that all surface waters collected and
treated in this 1M/IRA wUl be discharged to South Walnut Creek, just downgradient of CS-132.
6.1.2
Surface Water Treatment
The surface water collected will be treated using cross-flow membrane filtration (for suspended solids
and radionuclide removal), followed by liquid-phase activated carbon (for organics removal) (Figure 6-1). The
respective units and appurtenances wUI be housed in three 48-foot traDers to protect weather- or temperature-
sensitive components. Fire protection within the traDers will be provided by two wall-mounted, 25-pound, dry
chemlcal-type fire extinguishers. The traDers and all treatment units are constructed of non.:combustibles.
Other than minimal files and records. no combustible materials wAI be maintained within the trailers. Extemal
water pipes wUI be above ground and heat traced to protect against freezing. All tanks, piping and sumps will
be equipped with secondary containment to comply with 6 CCR 1007-3 and 40 CFR 264.193.
SURFACE WATeR INTERI'" REMEDIAl ACT10N PI..AN
ROCICV ~LATS PLANT. GOLDEN. COLORADO
eg&.; :-.-\_nUl\_~.mat
Marcn '991
-------
t
I'
~~~~~~~~u.J ,I
...............................-........-1 I
, I
I
I
I
I
I
I
I
-~~O!_------- ---_J
I
~
~
t :
~ING:
TANK: DRAIN TO
~ STORAGE ;/oNK OR
__1 NEurRAUZATlON
RECYCLE
STREAM
\NE MODULES
.
. . . . . . . . . . . . . . . . .. ................
NEUTRALIZA TION
I
I
I
I
1
: LEAD
I CARBON
! I COLUMN
! i :
i i, ,;; . . I !
: L.... ......... L....: 0 I
I
: OPERAllNG UNITS I
I i
L---I-~ ~ ~-~----I-J,pOUSHIN~-I----"
I CARBON . I CARBON I
COLUMN . I COLUMN I
L (ST,,",O-aY): I (ST,,",O-aY) i
! I
. -1 LJ L;
ON-liNE STAI'W-BY UNITS
POUSHING
CARBON
COLUMN
TREATED
WATER
(DISCHARGED TO
SOUTH WALNUT CREE!<
DRAINAGE JUST
DOWN GRADIENT OF CS-61)
.......,.......................,.. .
FIGURE 6-1
PROPOSED 1M/IRA TREATMENT SYSTEM
-------
10 I UU I .MtlCWoootN I :.!W
EQUAUZATION I
TANK I
CHEMICAL
PRETREATMENT
[eIPITA]J':ENTS
. I
CROSS-FLOW FILTRATION
. """"""""""""""""""'" .
SURFACE
WATER
INflUENT
. """"""""""""""""""""
RECIRCULATION
PUMP
,
I
I
I
I
I
I
I
I
I
I ~------p---------
i m ;
I IC~INd lEANING:
! L;J TANK; STO~~
~_____l______j NE~
CLEANING LOOP
MEMBRANE MODULES
REACTION
TAN;L
REACTION
TAN1
I I
CONCENTRATION
TANK
FEED EQUALIZATION
. """"""""""""""""""""""'" ................
. .. . . . . . . . . . . . . . . . . . . . .
SrntJNG
TANK
TOA
hi
. ~.
v:
TOA :
SOUDS TO DISPOSAL :
~EUTRAUZA TIONr;H\
ACID ~?!l
. I' "
: : I
: !: I
~ i~ /
: -/
: C>I.o
. """""""""""""""""""""""""""......... .
. ......,...,..........,
SOLIDS DEWATERING EQUIPMENT
-------
Major components of the treatment system include:
.
Exterior to the TraDers
...
.
.
(1) 10.()()().gaIlon equalization tank
piping
associated pumps, gages, and valves
.
Interior to TraDer 1
.
.
main chemical reaction system
solids dewatering system
Interior to TraDer 2
.
.
filtration system
process instrumentation system
neutralization system
.
Interior to TraDer 3
.
.
(2) 6O-inch carbon units
(2) 50-Inch standby carbon units
associated plastic (PVC) piping and valves
.
As the flows from the different sources are expected to. vary, the equalization tank will ensure a
somewhat constant flow and loading through the treatment system. The treatment system is designed to run
continuously at a maximum flow rate of 60 gpm. At peak flow, this tank wUI provide approximately three hours
of equalization detention time. The average annual influent flow rate. however. is estimated at approximately
20 gpm. Surface water collected during periods of these lower influent flow rates will be allowed to accumulate
in the equalization tank and then treated at the system design flow rates.
SURFACE WATeR IN'TCRlIol REIoIEOI4L AC'T1ON PI.AN
ROCXV FloATS PI.ANT. GO\.De/oi. COUJI'WX)
09&; ._,.p ._nUl.._~.mar
~arC:rI '99~
-------
6.1.2.1 SUSpended Solids and Radionuclide Removal
When the treatment is initiated. the water will be pumped from the surge tanks to Trailer 1. and
')
subsequently to Trailer 2. which contain all equipment, tanks. pumps. piping. valves. and instrumentation for
cross-flow membrane filtration. The system consists of totally integrated, skid-mounted and automatically
controlled units for maximum reliability and minimum operator surveillance. The system is divided into various
.
systems as described below.
Main Reaction Svstem
Radionuclides and heavy metals will be precipitated and/or adsorbed from solution in the main
reaction system. The reaction system will include two 1200-gallon tanks sized to ensure complete precipitation
or adsorption of radionuclides prior to gravity flow to the filtration system. Chemical metering pumps.
controlled by pH or Oxidation Reduction Potential (ORP) monitor/controllers, will ensure that optimum reaction
conditions are maintained automatically. The tank will be agitated with a heavy duty electric mixer. The
equipment provided in the main reaction system will be as follows:
.
(2) 1200-gaJlon. RFP reaction tanks;
.
(2) heavy~uty mixer;
.
(2) pH monitors/controllers; and
.
(2) chemical metering pump(s).
Ferric sulfate wOI be introduced to the first tank in a liquid solution. However, a system will be
provided to dissolve the powdered chemical reagent, for controlled introduction into the main reaction section.
In the powdered chemical make-up system, a covered tank will be periodically filled with water, and powdered
ferric sulfate will be added manually in a prescribed amount. A mixer will be provided to assure that the
reagent is completely dissolved before it is delivered by a metering pump to the main reaction system.
SURFACE WATER INTERIM REMEDIAl. ACTION PlAN
ROCKY FLATS PlANT. GOLDEN, COLORADO
89&9\-''81>\ walnul\sec-e.mar
March 1981
-------
Ume will be added to the second tank as a slurry to raise the pH. The elevated pH wUI cause
precipitation of the iron as ferric hydroxide and create conditions conducive to the adsorption of uranium and
.
plutonium. The lime slurry will be prepared by filling a tank with water and then manually adding a prescribed
quantity of lime to the tank through a chute. The mixture will be well agitated with a heavy-
-------
The concentration tank will be made of fiberglass reinforced epoxy equipped with appropriate baffles
and liquid level controls. The recirculation pump will be stainless steel for corrosion resistance and rated at
100 feet of head. The pump will be provided with water-flushed double mechanical seals.
..
The treated water will be filtered through tubular (10 diameter) filtration membranes made of
-
fluorocarbon polymer, and arranged in trains of 1 D-tube modules piped in series. supported on accessible
horizontal racks. Each module will be 6-feet long and 7-incheS in diameter, with a separate oUtlet for clean
effluent. ~ flow Indicating and totalizing meter wAI be provided on the effluent line. Manifolds will be provided
to collect the effluent and direct It by gravity to the neutralization system. The metaljradionuclide suspension
will be concentrated to a 2 to 5 percent slurry in the concentration tank, from which it will be periodically
pumped to the slurry holding tank and titer press in the slurry dewatering system. The slurry removal rate will
be adjusted manually to maintain the desired solids concentration in the filtration section. All piping and valyes
in contact with the water being treated will be heavy-duty, corrosion-resistant plastic.
Neutralization Svstem
A skid-mounted neutralization system wUI be provided to adjust the effluent pH to the conditions
required for discharge or recycle. The neutralization system will be sized to receive and treat the effluent from
the membrane filters. The neutralized effluent will leave the system by gravity. The equipment and
components of the neutralization system are as follows:
.
(1) 1500-gallon, heavy-duty plastic tank:
(1) heavy-duty rim-mounted mixer:
.
.
(1) metering pump for acid: and
SU~"CE W"TER INTERIM REMEOW. "CTIOfoj PI.AN
I'!OCI(V Fi.ATS~. GOlDEN. COLORADO
"9&;._,_\_n",.._~.mat
M&tcn ~ 9& I
-------
.
(1) separate control panel containing:
1 pH monitor/controller
~
1 pH recorder
pH out-of-speclficatJon alarm
electrical switches and eontactors.
,
Process Instrumentation SYStem
A central control panel with a National Electrical Manufacturer's Association (NEMA) 4 rating will be
provided to house all controls. electrical switches and disconnects. and motor starters. The main items will
include the following:
.
pH and ORP monitor/controllers/alarms;
.
Indicator lights, switches and alarms for major components;
.
Motor starters and circuit breakers for all pumps;
.
Seal water alarms;
.
Level controls and alarms; and
.
Effluent flow indicator/totalizer.
All wiring and controls will meet applicable national electrical codes.
Solid Dewaterina SYStem
The solids dewatering system wUI include a 4-cubic-foot filter press using an air-operated slurry feed
pump to feed concentrated waste slurry from the concentration tank to the filter press. The filter press will
dewater the solid to 35 to 50 percent solids. Based on the preliminary sizing, it is expected that the press will
be emptied once every five days. The filtrate produced by the filter press will also be directed back to the
SURFACE WATEF'lII'lT'EFalol FlEIoIEDIAI. AC1'1ON PI.AN
~ FL.4TS~. GOI.OEN. co<'ORA!)O
eg&g'._-,-".., ._~.",.,
Marc'" '99"
-------
concentration tank or the feed sump for reprocessing. The filter press sludge cake is collected safely and with
minimal worker exposure. An air blowclown system automatically removes the sludge cake from the press.
The cake then falls through sludge cake chutes mounted under the filter press (elevated) and into drums.
\-
Sheeting will be placed around the transfer equipment and drums for splash protection.
-
6.1.2.2 Organic Contaminant Removal
Organic contaminant removal by GAC is a considerably simpler process. After cross-flow membrane
filtration, the surface water will be pumped through two GAC columns in series, operated in downflow fixed-bed
mode (Figure 6-1). Two additional GAC columns wUl be In stock. Each carbon column is 60 inches in
diameter and 87 Inches high and contains 2000 pounds of carbon. Based on a flow rate of 60 gpm, the
hydraulic loading to each column will be approximately 3 gpm/tt2. Empty bed contact time for each colwnn
wUI be approximately 18 minutes. The columns are of stainless steel construction and will be interconnected
by flexible pipe with 2-inch carnlock hose connections. Once the column is drained of water, the unit is a
shipping container for returning the carbon for regeneration.
6.1.2.3 Effluent Discharge
Following treatment, the water wUI continuously discharge to South Walnut Creek just downgradient
of CS-134. Samples wAI be collected and analyzed twice per week. In the unlikely event of off-specification
processing or treatment process faiure, the treatment system discharge wUl at most return the drainage to its
pre-1M/IRA condition. In addition, detention, treatment, and monitoring at Pond B-5 provides a downgradient
safeguard.
SURFACE WATER INTERIM REItIECIAI. AC'T1ON "'-AN
ROO
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6.2
. OPERATION AND MAINTENANCE
.
6.2.1
Surface Water Collection
..
The collection systems are reiativeiy maintenance free. Manholes, sumps, and backwater pools will
require periodic cleaning to remove accumulated solids. Pumps will also require routine inspection and
maintenance.
6.2.2
Cross-Row Membrane Filtration
The cross-flow membrane filtration system's instrumentation and controls will monitor and automatically
adjust chemical feed rates. System levei switches wUl automatically operate the feed and process pumps to
allow for the continuous flow of surface water through the system. Interlocks and alarms will automatically shut
down the system If critical components are operating outside the design limits. Therefore, the system will be
capable of processing surface water with only minimal operator attention. However, operator attention required
for the system, estimated at less than two hours per shift. will include these tasks:
1.
Maintaining appropriate solids concentration in the concentration tank by adjusting the amount
of waste slurry feed to the dewatering section;
2.
Replenishing chemicals as needed;
Routine cleaning and calibration of pH or ORP probes; and
3.
4.
Periodically initiating the cleaning cycle and changing the cleaning solution. Typically. a
cleaning cycle takes less than 1 hour and Is carried out once every 40 to 80 hours of system
operation.
The filtration system includes a cleaning loop to provide for rapid convenient in-place cleaning of the
membrane surface. This includes two 500-gallon polypropylene tanks, an all-plastic cleaning pump (5 HP. '00
gpm at 80 teet of head) and appropriate valves and piping so that the periodic cleaning procedure can be
carried out conveniently and quickly. Actual operating experience will determine the cleaning frequency
SU~ACE WATER INTERlr.I REr.lEDIAI.. ACTION PIAN
ROCJo(V FLATS PlAHT. GOLDEN. ~
.;'.-.rac' _nU!'._~.rnar
MarcP\ , 99'
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required for optimum performance of the system. During the cleaning procedure, fresh water is used to flush
the waste slurry from the modules back to the concentration tank, and a cleaning solution (usually a strong
acid) is circulated through the modules with the cleaning pump for a few minutes. Finally, the cleaning solution
J
is flushed from the modules with clean water. Provision is made to reprocess the cleaning solution as part of
the normal waste stream so that only clean effluent leaves the system.
.
6.2.3
Activated Carbon
Operation and maintenance of the GAC system is also relatively simple. To completely utilize the
carbon, the columns will be arranged in series, allowing the lead column to become fully exhausted for
subsequent regeneration while the second (polishing) column ensures effluent quality. Periodic samples will
be taken from the effluent of each unit, and when the lead unit effluent exceeds chemical-specific ARARs, the
lead carbon column will be removed, the polishing (second) column will become the lead column, and a
stock carbon column will be put in service as the polishing unit. This is expected to occur every three weeks.
The carbon column with the exhausted carbon will then be shipped to an off-site location for regeneration.
6.3
ADDITIONAL DOCUMENTS
In addition to this 1M/IRA Plan, EG&G will also be preparing the following documents:
.
Site Specific Health and Safety Plan (SSHSP) for construction and operation of the 1M/IRA;
Community Relations Plan (CRP);
.
.
detaned design plans and specifications;
.
detailed "as-built" drawings incorporating all field changes to accurately reflect the constructed
surface water collection and treatment system; and
.
an Operation and Maintenance Manual (O&M) for the 1M/IRA.
SURFACE WATER INTERIM REMEDIAL ACTION PlAN
ROCKY FLATS PlANT, GOlDEN, COLORADO
eg&g\_irap \ walnut\ MC-6.m81
March 1991
-------
The SSHSP and O&M Manual will be prepared after the 1M/IRA design is finalized since these
documents provide project-specific procedures for construction and operating activities. The CRP will be
~
available for public comment on 30 January 1991 and will be implemented in August 1991.
6.4
TREATABIUTY STUDIES
...
A preferred surface water treatment system for the proposed 1M/IRA has been selected in spite of
several informational constraints. First, It is uncertain, although unlikely based on the available data, that
methylene chloride, vinyl chloride, and acetone are present within South Walnut Creek Basin surface waters.
Second, limited treatment technology performance data currently exist for removal of plutonium and americium
from natural waters. This is particularty true in the case of ion exchange. Finally, the physical state of
plutonium and americium (i.e.. dissolved vs. colloidal) In surface waters is not completely understood, nor have
the radlonuclides that contribute to the gross alpha and beta. activity been defined. The selected treatment
system is the logical choice given the avanable surface water quality data. literature information regarding
plutonium and americium chemistry and treatment processes for their removal, and best engineering
judgement.
However, treatability studies are appropriate to confirm the selection of the preferred treatment system
or to provide the basis for selection of an alternative system should the preferred system be judged to not
perform adequately.
The DOE wli conduct bench- and field-scale treatabDIty studies to determine the effectiveness of cross-
flow membrane titration, GAC, Ion exchange and other technologies in treating South Walnut Creek Basin
surface waters. Objectives of the bench-scale study Include determination of applicability of the treatment
technology, quantification of major operating parameters, evaluation of performance relative to meeting
chemical-specific ARARs and reevaluation of capital and operating costs. GAC wi/I be tested using a field
treatment unit which will be deployed in the northwest portion of the East Trenches Areas for treatment of
SURFACE WATER INTERIM REMEDIAL Ac:T1ON PIAN
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surface water from stations SW-S9, SW-61, and SW-132. The initial operational unit of the field unit is expected
to be Installed and started up in the Spring 1991. Because this first unit (the GAC system) will be used
primarily to demonstrate organic contaminant removal efficiencies. It will not be expected to attain chemical-
)
specific ARARs for metals and radionuclides by Itself. Additional units wUl be added over a several month
period to evaluate metals and radionuclides removal. Operation of this field-scale facUity will include testing
..
and modification of the original equipment as well as the addition of support equipment and/or alternative
troatment elements. A summary report of the treatabHity study findings wUl be submitted to the regulatory
agencies upon completion of the program. The results of these tests and the bench-scale treatability studies
may indicate that It is not practicable to attain all ARARs fOf the Surface Water 1M/IRA. Final performance
requirements for the 1M/IRA will require approval by the regulatory agencies.
SURFACE WATER INTERlIoI REMEOuu. AC'T1ON PI.AN
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SECTION 7
ENVIRONMENTAL EFFECTS OF THE PROPOSED INTERIM REMEDIAL ACTION
tI
The proposed surface water 1M/IRA, and potential subsequent environmental and human health effects'
'.
resulting from this action, are evaluated in this chapter. Environmental impacts to air quality. water quality,
terrestrial features (including wildlife and wetlands). archaeology and historic sites. and short- and long-term
land productlvtty are discussed In SectIons 7.1. 7.2. 7.3. 7.4 and 7.5, respectively. Human heatth exposure risks
from in_lation, routine operations. and accidents are analyzed in detalln Sections 7.6 and 7.7. These
analyses evaluate the risks to workers involved in the 1M/IRA. to other RFP site employees. and to the general
public. The commitment of resources (material/human), transportation impacts and cumulative impacts are
discussed in Sections 7.8 through 7.10.
7.1
AIR QUAUTY
There are three potential air quality impacts associated with the proposed OU 21M/IRA to selectively
collect and treat surface water within the South Walnut Creek Basin OU 2 from surface seeps and surface water
monitoring stations. These are:
1.
Potential VOCs released from exposed contaminated liquids during construction activities (Le.,
sump installation. trench excavation) or at surface water collection, storage, and treatment
locations, as part of nonnaI operations or accident conditions.
2.
Fugitive dusts and fossD fuel consumption related exhausts resulting from activities such as
excavation, construction. operations, maintenance. afld monitoring.
3.
Water treatment process off-gassing released to the environment as part of normal operations
or accident conditions.
Air quality impacts from VOCs released during construction activities (e.g., excavation) will be minimal
when compared to the normal operational activity at the Rocky Rats Plant. The .Phase II RFI/RIFS Workplan"
for OU 2 shows VOCs have been detected in the South Walnut Creek Basin soUs and include acetone (up to
500 ppb), and bis(2-ethylhexyt) phthalate (4,600 ppb) (EG&G, 1990a). Table A-10 in Appendix A presents the
SU~ACE WA"TCR INTCFII'" REMeow. ACTION
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test results for VOCs compied as part of this report. Due to their'isolated occurrence, and the limited amount
of excavation planned, the amount of VOCs released during this construction activity are not likely to cause
measurable changes In the ambient air quality. Based on sample analyses to date, VOC concentrations in soils
~
at South Walnut Creek are Insignificant. Consequently, normal construction activities and excavation for sump
installation, buried pipeline/utUlties and preparation of the pad area for the treatment system may not release
4
VOCs to the atmosphere. Preliminary characterization, based on the Phase I RI Report, indicates the presence
of elevated concentrations of semi-voiatUe organic chemicals (phthalates) In the soil. Any airborne releases
of semi-v,atUe organic chemicals wUl be from fugitive dusts associated with construction activities and will be
controlled as discussed below.
Dust associated with construction and operational activities wUI be controlled as specified in the
Environmental Restoration's Health and Safety Program Plan (ERHSPP). The ERHSPP addresses the minimum
health and safety requirements for outside contractors as dictated by the ER Department and the Health Safety
(HS) Department. The ERHSPP is in final form and is currently undergoing a final review by EPA and CDH.
The ERHSPP outlines the requirements for a project-specific or Site Specific Health and Safety Plan (SSHSP)
that Identifies construction tasks, potential hazards, and the steps to control hazards. The SSHSP will be
prepared in accordance with guidelines set forth in the ERHSPP, and wUl be completed after the 1M /IRA design
is finalized since this Plan provides procedures for specific 1M/IRA construction and operating activities. The
SSHSP must be approved by the ER and HS Departments, and will be reviewed by EPA and CDH.
Upon approval of the SSHSP, the outside contractor is briefed and assigned an RFP construction
engineer. This engineer Is responsible for construction management and implementation of the SSHSP by the
contractor. The HS Department wUl then issue a renewable one-week permit, conditional on the workers being
briefed and understanding the heatth and safety concerns of the construction effort. The construction is
monitored by the HS Department for contractor adherence to the SSHSP.
SURF.t.CE w.t.TE~ INTEl'll'" RE...eow..t.C'T1ON
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In addition to these requirements. the ER Department has developed wind speed and dust control shut.
down limits as guidelines for the 881 Hillside 1M/IRA SimUar project document guidelines will also be required
..
for construction of the South Walnut Creek Basin 1M/IRA at OU 2.
.
Dermal exposure, inhalation, and inadvenent ingestion of airborne radioactivity and VOCs on fugitive
dusts is analyzed in Section 7.6. "Personnel Exposure-Routine Operations", Pollution from engine emissions.
fugitive dust generation by vehicles and particulates from tire wear are analyzed separately in Section 7.9,
"Transportation Impacts".
Collected contaminated surface water will be processed through the proposed cross-flow membrane
filtration system and activated carbon system facUity. Due to the low VOC concentrations in the surface water,
the proposed treatment system will not produce measurable VOC emissions; therefore. no changes in Jhe
levels of these gases in the ambient air off site is expected. The need for periodic membrane cleaning will
require the use of a small amount of sodium hypochlorite (NaOHCI). This could occur once every 2 to 4 weeks
and wUI not impact off-site air quality.
The cross-flow membrane filtration system incorporated into the water treatment system to remove
suspended solids, dissolved metals. and radionuclides may not contribute to emissions during normal
operations or back flushing operations. Mixing of chemicals for water pretreatment or strong acids or bases
used for hardware cleaning operations may contribute to odors within the confines of the water treatment
trailers and should be controlled by adequate ventRatlon, These odors will not be noticeable from outside the
treatment facUlty area. nor will they be a hazard to workers in the traDers under normal circumstances, Spills
of chemicals that might be involved in accident conditions will be administratively controlled by actions
specified In the Operational Safety Analysis (OSA).
The OSA addresses health and safety concerns originating from routine site operations. It is similar
to the SSHSP In that health. safety, and environmental hazards are identified and evaluated for control. This
SU~ACE WATCFlINiEFIIM REMEOtAL AC'T1ON
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19&9 . ""r8,p ,..,nut'" Me" 7.mat
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analysis is also reviewed by and must be approved by the HS Department. Training is required prior to
operation with oversight and monitoring by the HS Department.
.,
Operation and maintenance of the GAC system are simpler than for the cross-flow membrane filtration
system. The GAC columns. containing exhausted carbon. wUl be shipped to an off-site location for
<8
regeneration. Spills of liquids associated with the operation of the GAC columns wUl be limited to the effluent
exiting the cross-flow membrane filtration system. which Will have removed many of the constituents of
concem. The effluent water from the membrane filtration treatment system may contain some amount of
VOCs. Effluent concentration requirements are contained in Table 4-1, Basis for Design of Surface Water
Treatment.
7.2
WATER QUAUTY
The proposed 1M/IRA will reduce the contaminant loading to South Walnut Creek. Surface water runoff
entering excavated areas and exceeding the design capacities of the system may create soil entrainment
(sediment transport) by surface runoff ending in open waters on site. The amount of water exceeding the
design capacity of the collection system should be minimal.
Some excavation will Occur in soDs that are expected to have measurable levels of semi-volatile organic
chemicals. primarily phthalates. Because phthalates adsorb onto the soD particles and thus are not transferred
from soil to water in measurable quantities. surface water runoff should not cause a water quality concern as
long as erosion control measures are applied to all soils excavated during remedial action. The 1M/IRA
construction specifications will Include post-excavation erosion control measures. Techniques may include,
but not be limited to fiber composite nets. grouted riprock. hydromulching. and seeding.
South Walnut Creek Basin soils within au 2 are contaminated with plutonium and americium (Rockwell
International, 1989a). Prior to construction work for the surface water contamination cleanup, surveys will be
SUI'IFACE WA':C~ INTEI'lIIoI REIoIEOIAJ. AC'l1ON
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performed to detect any presence of elevated radioactive contamination. Elevated radioactive contamination
wUI be handled In accordance with the SSHSP procedures.
-(
For the cross-flow membrane filtration system, the greatest potential for negative water quality impacts
..
results from chemicals involved in the pretreatment of the waste stream and concentrated acids or bases
utilized periodically for descaling of equipment. Handling of the concentrated cleaning chemicals will be
governed by an OSA. as will the precautions for handling the dewatered solids generated in the water treatment
process. -
Dewatered solids will be handled as a low-level mixed waste. This will require solidification at an
existing RFP facUlty to meet the transportation and disposal requirements. The solidified waste will be disposed
of at the Nevada Test Site or slmDar facUlty after it is sampled and analyzed to determine compliance with
recently promulgated RCRA land ban restrictions.
The volume of waste will not be a major addition to those wastes already processed at the RFP. The
collection, transport, and treatment of the dewatered solids wUI be in accordance with standard Plant operating
procedures and does not present a significant hazard to on-site or off-site water quality.
The GAC adsorption system will provide even less prospects for negative impact to water quality on
site than the cross-flow membrane filtration system. The carbon columns will be fully self-contained and hold
approximately 2,000 pounds of carbon. The units are shipped to an off-site location for regeneration.
Approximately one gallon of water per 3 to 4 pounds of carbon (500 gallons) could be spilled during unit
changeout of the carbon column. This possibility is mitigated by the use of secondary containment which
captures all of the potentially spilled water. The net effect Is that there will be no spill during carbon column
changeout. Procedures will be established for the safe changeout of the exhausted GAC columns. The
transport of the exhausted GAC columns will be in accordance with standard Plant and project-specific
operating procedures and presents a negligible hazard to on-site or off-site water quality.
SU~ACE WATER INTERIM REME~ AC'"nON
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7.3
TERRESTRIAL IMPACTS
Terrestrial environment features that may be negatively impacted by the proposed 1M/IRA include
'r
animal life. plant life, and land forms Oncluding wetlands). These negative impacts are expected to be minimal.
because of the disturbance to the areas of concern caused by the Plant's construction and operation during
..
the past 37 years. These past disturbances have left the 903 Pad with an asphalt pad cap and the East
Trenches Area has surface evidence of burial trenches. The effects of the 1M/IRA wUI not significantly impact
the already-
-------
The proposed 1M/IRA is not expected to have an adverse effect on linear wetlands. In 1989. EG&G
authoriZed the preparation of a wetlands assessment for the entire Rocky Flats Plant site (EG&G. 1990b). This
1
report Identified 107 acres of areal wetlands and 84,970 feet of linear wetlands within the Rocky Rats Plant site.
South Walnut Creek is identified as one of six ephemeral streams traversing the property and is considered
~
relatively important as part of the site drainage system. The proposed action, as It impacts wetlands. will not
be discernible from current stream management.
No wetlands impact is expected from treating water prior to reintroduction into South Walnut Creek.
The proposed action calls for withdrawal of up to 37.5 gpm of contaminated surface water from station SW-61 ,
4.5 gpm from SW-59, and 18 gpm from SW-132. Water from these collection points will be diverted into
properly sized sumps and piped to a treatment plant equalization tank to provide the treatment plant with a
constant feedstock. Water from the treatment plant wUl be reintroduced Into South Walnut Creek immedialely
downstream of CS-132. Water diverted from the sources would be removed from the surface water system
for no more than 3-4 hours at 60 GPM and for no more than 48 hours at very low flows.
As mentioned earlier, treated water from the treatment system wUI be discharged into South Walnut
Creek, just downgradient of CS.o1 (the surface water collection system of SW.o1). The South Walnut Creek
basin contains a series of five on-channel reservoirs. The last pond In the series. Pond B-5, discharges directly
into South Walnut Creek. Water volume is managed by these ponds and is discharged directly to South
Walnut Creek in accordance with the Plant's NPDES Permit. Discharged water follows the South Walnut Creek
drainage north to the natural Walnut Creek drainage. Surface water flow in Walnut Creek near the property
boundary is currently being diverted around Great Western Reservoir, which is a drinking water source for the
City of Broomfield, and is then returned to the natural drainage channel. Due to the ephemeral nature of South
Walnut Creek, no impact to wetlands is anticipated as a result of the proposed action to treat surface water.
Although no long-term impact to wetlands is anticipated, It is possible that construction activities could
adversely affect a few wetlands plants during ditch modifications or sump installation. Replacement of any
su~...ce W"'TE~ INTER!'" RE"'EOIAl AC'T1ON
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destroyed wetland plants wUl follow the completion of construction, resulting in no net impact to wetlands at
the RFP.
t
7.4
ARCHAEOLOGY AND HISTORIC SITES
k
The 903 Pad, Mound and East Trenches Areas have been highly disturbed over a number of years.
Due to this disturbance and the topographic position of the subject area, the State Office of Archaeology and
Historic ~reseN8t1on has determined that this action will not Impact cultural resources (Burney, 1989).
An archaeological and historical survey of the RFP was conducted between July 18 and August 22.
1988, which determined two sites have potential eligibnlty to the National Register of Historic Places. However,
insufficient information currently exists to make this determination. These two sites are located northwest and
soUthwest of the investigation area, and wUl not be disturbed by the proposed action (Burney, 1989).
7.5
SHORT- AND LONG-TERM LAND PRODUCTIVITY
Land within au 2 is currently undeveloped and will remain so for the foreseeable fUture as part of the
Rocky Flats Plant. au 2 lies within the Rocky Flats Plant security boundaries and is not accessible to the
general public.
7.8
PERSONNEL EXPOSURES - ANALYSIS METHODOLOGY
The effects of personnel exposures to hazardous chemicals have been estimated in terms of increased
risks of either developing cancer (carcinogenic risk) or some other adverse health effect due to the exposure
(noncarcinogenic risk). Analyses were done separately for those directly involved in remedial actions (workers),
other RFP personnel not directly involved in remedial actions (site employees), and off.slte individuals (general
public). Detailed risk assessment calculations are provided in Appendix G.
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Airborne contaminant concentrations at the receptor (site employees, general public) locations were
estimated using the Gaussian Plume Equation of Pasquill as modified by Gifford (1961) for ground-level
-
concentrations at the centertlne of the plume. Assuming a ground4evel release, the equation becomes:
x/a
=
(K (ly (lz u)"'
.
Where:
x = air concentration, mg/m3 or cijm3
Q = emission rate, mg/sec or ci/sec
u = wind speed, m/sec
(ly = horizontal dispersion coefficient, m
(lz = vertical dispersion coefficient, m
The dispersion coefficient value is a function of the downwind distance, whether the contaminant
emission Is a long-term (construction, operation) or a short-term (accident source), and the prevailing
meteorological conditions (PasquDI StabOity Class). Long-term dispersion coefficients were calculated using
.
Briggs formulas for open country conditions (Gifford, 1976), PasquUI Stability Class D (prevalent condition per
RFP EIS), and average annual downwind directional frequencies. Short-term dispersion coefficients were
calculated using formulas developed by Slade (1968), Pasquill Stability Class F, and no wind directional
averaging.
The toxicity assessment (intake and risk) for carcinogenic and noncarcinogenic effects of chemicals
was performed in accordance with the EPA's Risk Assessment Guidance for Superfund Sites (EPA, 1989).
EPA's Integrated Risk Information System (IRIS) was utUized as the primary source for toxicity information
(RFDs and slope factors). EPA's Health Effects Assessment Summary Tables for the fourth quarter of FY 1990
(EPA, 1990b) were used as a secondary source of information. For organic chemicals, inhalation toxicity
values (RFDs. slope factors) were estimated using the oral pathway values in those instances where inhalation
values were not avaBabie. It would be expected that the toxicity values for both pathways would be similar
due to similar absorption efficiencies for organic materials.
Estimates of carcinogenic risks were calculated for each of the organic chemicals identified in Table 4- 1 ,
and the individual risks summed for a total carcinogenic risk. The carcinogenic risks are considered to be
SURFACE WATE~ IP,_n\l! ._.7."'"
Marc:1" '991
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cumulative for the entire period of exposure and the calculations yield an estimate for the lifetime increased
risk of cancer.
..
Noncarcinogenic risks are considered 'hreshold" events. That is. no effect is observed below a given
exposure. The potential for increased health effects are expressed In terms of the non-cancer hazard quotient.
.
which equals the exposure level divided by the reference dose (noncarcinogenic toxicity value). The EPA
methodology assumes that a quotient value of less than one is unlikely to result In adverse health effects. even
for sens~ive popUation groups. Generally, the greater the quotient value above unity, the greater the level of
concern. Chronic or subchronlc reference dose values were utDiZed in the non-cancer hazard quotient
calculation, depending on the potential duration of the exposure.
Exposures to site employees and members of the general public were analyzed based on a single.
hypothetical individual for each exposure category. Site employees were assumed to be assigned. eight hours
a day for the duration of the release, to whatever buDding would receive the greatest average airborne
exposure. For the proposed action, the nearest occupied locations resulting in the greatest exposure to other
site personnel include BuDding 988, 995. and the Gate 9 guard post Onner guard post on east access road).
The analysis of the Impact to the general public assumed a single Individual would remain at the point of
highest exposure (due east at Plant boundary) accessible to the general public for each pathway, twenty-four
hours per day, for the entire duration of the release. These calculations provide an upper bound for the
increased risks to an Individual from each of these groups. During the remedial action. It Is unlikely that any
worker, site employee, or member of the general public would exceed or even approach the risks estimated
for their respective group.
In calculations of the estimated increased risks to members of the general public from hazardous
chemicals. the impacts on infants and young chDdren were calculated separately from those on adult members
of the population. Infants and young children differ from adults in the rate of uptake of the hazardous
chemicals and In body weight. Both of these factors influence the calculations of increased risk. To assess
noncarcinogenic risks. non-cancer hazard quotients were estimated for both children and adults. The numbers
SURF4CE WA'TER INTER'" REMEDIAL A~
'O:I(Y FLoATS P\.NlT. GOI..OEN. OOI..OAAOO
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quoted In the text of this document are those for the group with the greatest increased risk or concem.
Carcinogenic risks to a member of the general public were estimated assuming exposure for the entire length
.(
of the release, which was conservatively assumed to be thirty years. Two exposure categories were
considered: 1) the member of the public is already an adult when the project starts; and 2) the individual
..
Is assumed to be a child for the first five years of remedial action and an adult for the remaining 25 years. The
numbers in the report represent whichever analysis yielded the highest Increased risk of cancer.
The intake of radioactive materials has been assessed by calculating total intake by individuals and
converting that to Committed Effective Dose Equivalent (CEDE) using the exposure-to-dose conversion factors
for Inhalation (Table 2.1 of EPA, 1988). Internal Dose Conversion Factors for Calculation of Dose to the Public,
Part 2 (DOE, 19888), was used to assess dose to the public. The calcuiated exposure values are then
compared wtth the applicable DOE limits for each receptor group. DOE Order 5480.11 (DOE, 198Bb)
establishes a limit of 5 rem (eHective dose equivalent) per year for occupational workers. DOE Order 5400.5
(DOE. 1990b) Incorporates a Oean Air Act (eM) limit of 10 mrem (effective dose equivalent) per year for
members of the public from routine airborne emissions and a dose limit of 100 mrem per year from all
exposure modes.
7.7
PERSONNEL EXPOSURES - ROUTINE OPERAT10NS
7.7.1
Worker ExDOSure Risks
Workers invotved In the Installation of collection facUlties and those Involved in operation of the facilities
associated wtth the remedial action may experience increased risks through several pathways:
1.
Airborne exposure to VOCs near construction activities. equipment installation. or within the
facUity.
2.
Dermal exposure to organic and inorganic chemicals or radioactive materials. especially during
construction activities.
S'-IRFACE WA'TER IJolTERIIoI REMEDIAL ACT10N
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3.
Inhalation of organic chemicals, inorganic chemicals, or radioactive materials on fugitive dust.
especially those generated during construction activities.
~
Airborne Excosures to VOCs
..
It is proposed that the treatment facUlty be located In the East Trenches Area, nonhwest of IHSS.' '0.
Associated piping and utUities wBI be located, to the degree possible, to avoid soils contaminated with VOCs.
There will be monitoring to assess possible exposures to VOCs during these construction activities. Protective
measures appropriate for the level of VOCs detected wit be specified In the SSHSP to protect the workers.
The potential for chronic or routine exposure of workers to VOCs resuttlng from operations and maintenance
tasks will be small. OSA procedures will be established to control potential hazards to workers.
The treatment facUlty traDers will be ventUated to prevent the buUdup of VOC vapors in the work
environment. The process reaction, concentration. and neutralization tanks wDI be equipped with hinged
covers to minimize the introduction of VOC vapors into the work area. The filtration, dewatering, and carbon
adsorption units are closed systems and thus will not act as VOC vapor sources. Periodic (every' to 3 days)
removal of dewatered solids (sludge) from the dewatering equipment will be necessary. This will require
opening of the filter press housing and potential short-term exposure to VOC vapors. FacDIty ventilation and
OSA procedures wil provide appropriate personnel protection. The wet consistency of the sludge will preclude
potential aerosolization of radioactive particulates and associated exposure from inhalation. The dewatered
solids will be handled.8$ a low4evel mixed waste. Outdoor operational tasks, such as maintenance of the
surface water collection system. will be performed in accordance with the appropriate OSA.
Activities that might lead to nonroutine exposures, such as opening tanks or other maintenance
operations, WIll be of short duration and will not lead to chronic exposures. Monitoring these activities will be
necessary. however, to determine that adequate protective measures were used to assure that workers were
not exposed to VOC levels exceeding appropriate limits for the individual chemicals.
SU~ACE WA'!EFlINTEFllt.I REIoIEDW. AC'T1ON
~ ~""'TS "'.»(T. GO\.DEN. COI.ORAOO
89&; ""'4~ .-.",\.1\ ,IIK-?mat
Uar:!'" 199'
-------
Dermal ExDOsures
{'
As with airborne exposures, potential dermal exposures will be controlled with the implementation of
SSHSP and OSA procedures. Potential levels of protection from splashing and contact with contaminants
..
include the use ~ gloves, protective clothing, goggles, and hoods.
During construction activities for the proposed action, there will be little or no potential for dermal
contact with soli contaminated with VOCs. The treatment facUlty will be constructed In the East Trenches Area,
northwest of IHSS-110, where VOC contamination levels are anticipated to be low. The piping for the water
treatment facility will be routed through uncontaminated so8 to the extent possible. Any excavated soil from
designated IHSSs will be treated as a RCRA mixed waste untY determined otherwise. Inorganic chemicals and
radioactive materials identified In the work areas are not readUy absorbed through the skin and would re$ult
in a negligible exposure pathway.
Personal protective measures may be necessary during some routine operations activities where there
Is a potential for contact with contaminated water (e.g., routine water sampling or solids removal in the
treatment facUlty). If such measures are necessary for the protection of the workers. they will be specified in
the OSA for those activities.
Inhalation of Fualtive Dust
Fugitive dusts are likely to be generated during construction activities for the water collection and
treatment facUlties. The Phase II Sampling Plan (EG&G. 1990&) Includes soH sampling in the areas of interest,
but the resutts are not yet available. For this reason, the surface soU conditions have been estimated using
available soU samples from the Phase I RI/FS (Rockwell, 1987a). Where soU samples were not available, the
nearest soU samples located between the area of interest and the most likely source of contamination have
been used.
SURF ACE WATER IN'TCFlIoI FIOIoIEOIAI. ACTION
~ocv ~"""TS "I..A/oIT. GOI.DEN. CO-OF\AOO
.;.&.Q ."IIW) .-..nl.lhll8C.7.mat
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-------
The soil sample results indicate that the only organic chemical of concern in soil above the water table
is bis-(2-ethythexyl)phthaJate. Acetone and methylene chloride were reported but are suspected to be
laboratory contaminant artifacts. Consequently, It is the only significant organic chemical contributing to
\
carcinogenic and noncarcinogenic effects from the fugitive dust pathway. The radioactive contaminants of
concern from the fugitive dust pathway include plutonium and americium. The contaminant levels in the
~
surface' soils for C$-59, O$~1, 0$-132, and the treatment facUlty are based on data from the nearest available
borehole.
Dust control measures will be specified in the SSHSP to limit Inhalation exposures to workers involved
in construction activities. These measures will be derived from the PPCD. Even If workers were to be exposed
to the maximum dust loading permitted by OSHA regulations for nuisance dust during the entire period of
construction activities, the effects of either fugitive radioactive material or phthalates would be insignificatlt.
The contaminated surface water collection stations will have surface piping routed to the treatment
facUlty. Consequently, transfer of contaminated surface water by tanker truck will not be required and will not
result In a fugitive dust source term during operations. Occasional travel to the surface water collection
stations will be required for maintenance or surveillance purposes. WhOe some fugitive dust may be generated
in the wake of the vehicle, It Is not expected to be a significant exposure pathway for the vehicle operator or
other construction personnel.
-
7.7.2 Site EmDlovee Excosure Risks
Other workers at the RFP site could be exposed to low levels of VOC vapors released during normal
operation and to fugitive dust generated during Installation and operation of the facilities associated with the
proposed action.
Although the vent on the feed equalization tank (see Figure 6-1) on the water treatment facility will have
an activated charcoal filter attached, in order to estimate an upper bound to personnel exposure, a calculation
SURFAce WATER INT;:"Iu,1 REMEDIAl. AC'1'1ON
RQCI
-------
was performed to detennine the potential VOC releases from the vent without a filter attached. Since that tank
is the largest single tank in which untreated water is collected. It was chosen as the tank which. if unfiltered.
.(
could lead to the greatest exposures to other site employees or the public. Any other tanks. sumps. or pump
vents would lead to lower exposures and lower risks. In the calculation. It was assumed that the liquid in the
.
tank was at the contamination levels listed In Table 4-1 and that the vapor In the tanks had reached equilibrium
with the liquids. It was further assumed that the vapors are displaced by in-ftowing liquids at an average rate
of 60 GPM. the design processing rate. That Is. It Is assumed that the average liquid Inftow must equal the
processing flowrme. but no credit was taken for water being removed from the tank.
Under these
circumstances. the maximum total cancer risk and total non-cancer hazard quotient would be very low.
There will be dust generated during the construction of the water collection facUlties as well as the water
treatment facUlty. Although dust suppression measures will be implemented In accordance with the PPCD and
SSHSP. the following conservative analysis. which assumes no dust suppression measures and high estimates
of areal disturbance and construction time. has been used to estimate health risks from dust generation. The
dust generation rate was estimated using the construction generation rate eX 1.2 tons per acre per month
(average soil moisture conditions) from AP42 (EPA, 1985). AP-421s an EPA document for estimating source
terms for air pollutant emissions. It was assumed that the project would create dust over an average area of
one acre for two months. This multiplication led to a calculated average generation rate of 4.2 x 1004 kg of dust
per second. To be conservative in calculating the exposure of site employees. It was assumed that all the dust
was generated at the surface water collection stations. since this would produce the maximum exposure to
personnel at Buldlngs 988 and 995. The approach utDlzed to estimate surface contamination levels
contributing to fugitive dust has been discussed In the fugitive dust portion eX Section 7.7.1 of this report.
Using a wind dlrectJon weighted dispersion factor (X/Q) from CS-134 to BuUdlngs 988 and 995 of 2.43 x 1004
seconds per cubic meter, It is estimated that an Individual assigned to the buildings for the full sixty-day
duration of the construction activities would receive a maximum dose of 0.4 mrem CeDe from radioactive
materials In the fugitive dust. The corresponding incremental cancer risk and norH:ancer hazard quotient due
to the presence of phthalates and metals in the dust were calculated to equal 3 x 10. and 4 x 10-3. respectively.
SURFAce WATER INTERIM AEMeow. AC'T1ON
~ -L..4TS PI.ANT, GOI.OEN, COlOlWX:
'96Q '~\-""ut"88C.7.m8t
Marc" '99~
-------
As noted previously, the only potential fugitive dust source tenn associated with Interim action operation
is occasional travel to the surface water collection stations for maintenance or surveillance purposes. Due to
the Infrequent nature and short duration of any travel to the collection stations. chronic exposures to other site
~}
personnel from fugitive dust are not anticipated.
.
7.7.3
Risks to Members of the Public'
Members of the public could be exposed to the same sources of risk as described In the previous
section for other RFP site workers. The airborne concentration of the fugitive dust would be less for members
of the public because of the greater dispersion distance from the source.
The public may be exposed to fugitive dust containing phthalates. and plutonium generated during.1he
construction phase of this action. The maximum dose to a member of the general public from radioactive
contaminants present In dust generated during construction activities would be about 2 x 10-3 mrem CEDE.
This is very low and well within airborne exposure limits of 10 mrem per year to any member of the general
public (DOE. 1990b). The maximum incremental cancer risk to a member of the public due to phthalate and
metal contamination within the dust was calculated to be negligible during construction. with a value of 6 x 10-8.
The corresponding non-cancer hazard quotient was calculated to equal 8 x 1 O~ for construction activities. As
discussed in Section 7.7.2. some fugitive dust may be generated in the wake of vehicles traveling to the water
collection stations during normal operations for maintenance or surveillance activities. Due to the infrequent
nature and short duration of this travel and the distance to the plant boundary (approximately 1 mile), any
public exposure Is expected to be insignificant.
As discussed in section 7.7.2. potential VOC releases from the feed equalization tank were analyzed
to provide an upper bound on the risks from releases from other. unfiltered tanks.
Using the same
Throughout this report the term "general public" hu a special and very reltric:t8d meaning. In order to estimate the maximum
exposure or risk to any individual outside of the RFP lite. all estim&t81 are bu8d on exposure to a person at the site boundary
location having the highest a\l8rag' airborne concentration who remains there for 24 houri ,ach day. 365 days ,acn year. for
the duration of the operation or the rem'dial action.
SU~Ace WATER IN'TERIM REMEDIAL ACTION
~ .\oATS "'..ANT. GaDEN. co..ORADO
.. _''''''.-'''''188C.7.m8t
Maro" '9.'
-------
assumptions as described in section 7.7.2. the maximum cancer risk and non-cancer hazard quotient for a
member of the public would be very low.
{
7.8
PERSONNEL EXPOSURE - ACCIDENT
.
Any accidents that may occur during the construction phase of the proposed action are those typical
of small excavation or construction activities. The SSHSP wli identify appropriate precautions and
responsil:?illtles for each Job. Workers wUl be tamliar with the SSHSP and a copy of It wUl be available at the
work site. No credible accident during construction would lead to exposure of either workers. site employees.
or members of the public to levels greater than those res~ng from the severe accident case analyzed below.
During operation. accidents that could Impact either workers or members of the public would incl~e
fires or major spUls of contaminated material. Splls of untreated water wtthIn the treatment facility would create
the potential for short duration airborne VOCs. Uptake of contaminants by workers involved in the cleanup
would be controlled by following safety precautions specified in the OSA Any airborne VOC releases through
ventilation systems that could lead to exposures of other RFP employees (site employees) or the general public
would be less than the tank rupture discussed later In this section.
The Initiation and propagation of fire within the treatment facllty Is a credible accident. The facility
traDers are equipped with chemical fire extinguishers; however. the traUers wli not normally be occupied once
operations become routine. Any VOC releases would be bounded by the severe accident case since
concentrated VOCs woUd be contained within the acttvated charcoal columns which are closed components
and filled with water. Solids which are in the filter press housing or which have been removed and placed in
metal containers constitute a potential radioactive material source tenn. A fire would have to both dry out and
aerosolize the solids as well as breach the metal containment to reBUt In a radioactive release. Since the
solids are Inorganic and in a sludge form containing 60 to 70 percent water and are within metal containers,
and the traDer Is the only major combustible material present, It Is concluded that the fire duration and intensity
would be insufficient to result in a radioactive material release resulting in any significant impacts.
SURFACE WATCR INTER'" REMEDIAL -'C'T1ON
CIOCI(Y ~~TS PVM'. GOlDE", COLORAOC
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Marcf"l 1 99~
-------
If any workers were present during an accident Involving the rupture of the inlet tank, the danger of
traumatic Injury would be a greater concern than intake of hazardous chemicals or radioactivity. The
radloacttve materials present In the water are not volatile, nor are they readly absorbed through the skin. so
they do not present an ingestion hazard to the workers at the scene of the incident. The organic chemicals
')
are low In concentration and would not voiatUlze Immediately. Thus, whle the airborne concentration levels
.
near the tank would be higher than off-site or other on-slte locations. the workers would be aware of the
incident and would either evacuate or take protective actions. thus limiting their total exposure to the hazardous
material..
7.1
COMMITMENT OF RESOURCES
The scope of the proposed 1M/IRA is small and the resources (material/human) for construction and
operation of this surface water treatment system will likewise be relatively small. No significant commitments
of valuable resources are Involved.
WIth the exception of the land area. all of the materials for construction and operation of the water
treatment system will be irrevocably and irretrievably committed to the Implementation of the remedial action.
Most of these resources are normally consumed at the Plant at a rate which makes the requirements of the
remedial action Insignificant. The water pretreatment chemicals and cleaning solutions are already in use at
the RFP. The chemicals for the cross-flow membrane treatment system and the carbon canisters are all readily
avaUabie from oIf-site sources. Process chemicals, cleaning agents, and carbon wUl all be available within the
Denver metr~1tan area.
7.10
TRANSPORTA~ONIMPACTS
Human health impacts normally incident to transportation Include vehicle emissions in addition to
possible traumatic injuries and fatalities resulting from vehicular operations.
SURFACE WATER IN'TB'W REMECIAL AC'TION
ROCI(Y FLATS F"..N(f. GOl.OEN. COLOIWX:I
8Q6Q'. -- ..-"I.11\_.7.mar
"'&I'c:n 198'
-------
Normal transportation produces engine emissions. fugitive dust generated by vehicular traffic on
unpaved surfaces, and particulate from tire wear. The table below presents an estimate of emission rates for
(
the operation of a typical truck.
6
TRUCK EMISSIONS RATE
Pollutant
Hydrocarbons
Emission Rate fibs/100 aaI. fuel)
13.1
NOx
286.0
SOx
31.2
co
123.5
TSP
17.7
The Impacts on health resulting from transportation during the proposed action includes the poteAtial
for both pollution- and accident-related Impacts. The table below presents estimates of risks resulting from
truck transportation (Rao. 1982).
HEALTH EFFECTS PER KILOMETER
Source
~
* LCFs
Injuries
Fatalities
Pollutants
Truck
1.0 E-7
Accidents
Truck
5.1 E-7
3.0 E~
* LCF = Latent Cancer Fatality
UncertalntJes are associated with pollution emission rates and atmospheric dispersion behavior. To
compensate for these uncertainties. the analysis used conservative estimates for determining pollution health
effects. The tabulated accident Impacts are average values over all popUatIon zones (urban, suburban, rural)
and are derived from nationwide Department of Transportation (DOT) statistics.
The proposed action wUI involve transportation activities during the construction phase as well as during
subsequent operations. All construction shipments are anticipated to be made mostly by truck and wili
SURFACE WATER INTCRIIoI REMEDIAL AC'T1ON
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Marc'" '9&~
-------
originate within the Denver metropolitan area (within a SO-mAe radius of the Plant site). Materials to be brought
on site Include the treatment systems, storage tanks, piping, concrete, and associated equipment. The delivery
of these material. wi! require several truckloads over the construction period, followed by routine maintenance
travel between collection areas and the treatment facilltle8 (estimated at less than 50 miles per week). The
}
resulting transportation Impacts will be smail as seen from the tabulated emissions and health effects estimates.
To place transportation Impacts to the general public in perspective. It Is observed that approximately 60.000
.
round-trip truck shipments (one-way distance of 50 mUes) would be required to resutt In one additional latent
cancer fatality (LCF). An average of 210,000 truck shipments woUd be required to resutt In one additional
traumatic fatality. The increase in site travel during construction may be noticeable but will be of shon
duration. Outside the Plant boundary, the increase will not be noticeable.
Treatment of contaminated surface water from OU 2 wli r~ in an Incremental increase in site pickup
and deliveries of spent carbon columns and replacement units and chemic81s for the pretreatment of water for
the cross-flow membrane treatment system. Deliveries wli be spread out over the course of the year and will
be handled by one of the existing Plant chemical suppliers. The very small number of shipments involved for
both the carbon columns and the cross-flow membrane treatment system will result in an insignificant impact
to human health.
Off-site transportation Impacts associated with the shipment of solidified fitter sludge to a mixed waste
disposal site. such as the Nevada Test Site, wDI be very low as determined In DOE (1990b). Relatively low
concentrations cA contaminants. the physical form of the waste. disposal site waste acceptance criteria. and
compliance with DOT packaging and transport requirements all contribute to very low health effects from
incident-free shipment and accident events.
Operational activities wDl also include periodic Inspection of the collection system to remove debris or
other obstacles. as well as routine inspection of the pipeline collection system providing direct feed to the water
treatment facUlty. This wUl require vehicular travel to each collection station area. which is estimated to total
SURFACE w...~ INT9WwI REloIeow. AC'T1ON
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-------
10 to 15 mles per week. Impact to human health Qatent cancer fataJltjes from vehicular pollution) will be
negligible.
{
7.11
CUMULA~IMPACTS
.
Routine processing of the surface water collected from the surface seeps and drainages will result in
some additional solid wastes being generated from the site. Generation of flter press cake by the cross-flow
membra~ fItratIon system Is estimated to be a maximum of 70 cubic yards annually. The filter cake will be
treated on site and shipped to the Nevada Test Site or simler facllty for final disposal. The annual production
rate of the semisolid wli average much lower. All gaseous releeS88 wli be undetectable off site. None of the
materials that may be releesed are expected to be cor_.tIlltted by any natural process.
The drying of the semisolid sludge waste from the treatmenI system will require an increase in Plant
solidification operations to dry and package the waste for transport to a final disposal site. Neither the drying
nor packaging requirement wli add significantly compared to the current wor1doad of the facUlty. Radionuclide
accumulation in the sludge Is not expected to exceed exempt quantitJes by weight, so that shipment of the
sludge Is not expected to cause any special concern or require unusual controls.
It Is estimated that four workers wli be involved In routine operation and maintenance of the surface
water collection and treatment facllty. This wli have negligible Impact on the worldoad of Plant personnel.
In routine operations, these workers wli not be exposed to any levels of chemicals or waste stream pollutants
that would resIrict them from other assignments at the RFP.
Construction actMties will r.ut In increased vehicular traffic, engine emissions, and the number of
workers. The number of personnel required for the proposed action wit be a small Increase to the assumed
year1y additional construction loading.
SURFACE WA TEI'I1NT1::I'W FIEIoIEDIAL ACTION
ROCI
-------
-------
SECTION 8
ENVIRONMENTAL EFFECTS OF THE ALTERNATIVES
{
The preferred alternative and the proposed action for this interim remedial action is to gather
.
contaminated surface water from a series of point sources, transfer the collected water via pipeline, and
process the water through a water treatment system. The preferred treatment system consists of a cross-flow
membrane treatment system for removal of radlonuclldes and metals, followed by a carbon column system
for removal of VOCs. The treated water will then be returned to South Walnut Creek.
Several alternatives to the proposed 1M/IRA were evaluated for environmental effects. The alternatives
included: 1) no action; 2) surface water collection at Pond 8-5 and 3) ion exchange, granular media filtration
with polymer addition. UV peroxide oxidation, and air stripping. The alternative of surface water coIlection,at
Pond 8-5 has been eliminated based on the potential of generation of additional contamination and additional
volumes of water requiring treatment (See Section 4-1). Each remaining alternative is evaluated in regard to
environmental quality, personnel exposure and transportation impacts. Following the alternative evaluation,
Table 8-1 compares the potential Impact of the proposed action with the alternatives.
8.1
ENVIRONMENTAL EFFECTS OF NO ACTION
Although the no action alternative Is In direct conflict with the lAG reached among DOE, EPA. and the
State of Colorado, It Is discussed herein.
8.1.1
Environmental Oualltv
The No Action alternative would not involve any short-term impact to the environment or the work
force/general population and would eliminate the need for off-site transportation activities. However, it would
not contain nor remove any radlonuciides, VOCs or Inorganic contaminants. The No Action alternative would
pose a long-term release risk to the general public and would require remedial actions in the future.
SURFACE WAT'EFI INTERlIoI r:aeIolEOIAL. ACTION PlAN
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Marc:1"\ 199'
-------
The No Action alternative would require that the current quarterty site monitoring be continued.
Because the monitoring Is a part of the existing plant environmental monitoring program, the impact on plant
operations and the surrounding community would be effectively zero. However, because off-site migration
~
may occur in the future, the No Action alternative is unacceptable.
.
8.1.2 Personnel ExDosure
T~ No Action alternative wDl have minimal Impact on currem workers at the site or at adjacent sites.
Workers would stOI be required to collect quarterty sampling, which would presem no additional impact above
currem impact levels. The sources of hazardous materials would neither be removed nor comrolled. However,
the posslbUity of releasing contaminated water off-site would increase over time. The site would then be a
source of public exposura In the long term.
8.1.3 Transcortatlon
Since no remedial action would occur under this alternative. there would be no an-site or off-site
transportation activities associated with this alternative or related impacts to workers or the general public.
8.2
ENVIRONMENTAL EFFECTS OF ALTERNATIVE 2
8.2.1
Environmental QualItY
A variety of treatment technologies were investigated as alternatives to the proposed au 21M/IRA.
These included granular media fBtratlon with polymer addition for suspended solids removal and ion exchange
for metals and radionuclide removal. In addition, UV peroxide oxidation and air stripping with off-gas treatment
were examined for organic comaminam removal. Ion exchange and UV peroxide systems are proposed for
treatmem of comamlnated ground water at the 881 Hillside Area which comain constltuems which are similar
to the OU 2 surface water comaminants. However, with regard to ion exchange, plutonium is not a ground
SURFACE WATeR INTeR!'" RE...EOIAL AC"T1ON ~
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-------
water contaminant at the 881 Hillside Area. and ion exchange (or other inorganic treatment technologies) are
not proven technologies for removal eX plutonium for natural water. There 15 no appreciable difference in
{
environmental Impacts eX the alternative organic contaminant treatment technologies. The cross-flow
membrane filtration system is the only proven system for removal of the targeted radionuclldes.
.
8.2.2 Personnel Excosure
The use of alternate treatment technologies would have little Impact on the personnel exposure
associated with surface water cleanup. The contaminants in the water remain the same and the removal
techniques are essentially simUar with respect to personnel exposure a risk.
8.2.3 TransDOrtatlon
The selection of one of the other atternatlve treatment technologies may require different transportation
requirements, dependent on the rate eX water treated and the contaminants to be removed. The ion exchange
columns utDlze resin beads that may require periodic replacement. Using a UV peroxide treatment process
would reduce transportation Impacts primarily due to elimination of some of the by-product materials produced
by the process. Overall, the transportation Impact for this alternative is minimal.
8.3
SUMMARY
The Impacts of the altematlves are judged to be small. The potential impacts associated with the
proposed action and each eX the identified alternatives are presented in Table 8-1-A and B.
SURFACE WATa\ I~FI" REr.tEOIAL AC'T1ON P\-'N
~"Y Flail PIartt. ~. ~
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-------
f.~~
.,~i
I i~
- I ~
I. ~
lfi
I II
~
~
~
u t
~ ~
..."
;. II?
TABLE I-t-A
SUMMARY COMPARISON 0' POTENTIAL IMPACTS 0'
PROPOSED ACflON AND ALTERNATIVES. RADiONUCLIDE TREATMENT
Impact Cat~,ol)'
Alternatives
Proposed Action
No Action
Contact P'dtration/
Ion P.~hllQ8e
ENVIRONMENTAL IMPACTS
Excavation
Topographical Deformation (Perm8DCnt)
Endangered Species
Wetlands
Negligible None Negligible
Treatment Pacility None Treatment Pacility
Negligible None Negligible
Negligible None Negligible
Negligible None Negligible
Negligible None Negligible
Umited None Umited
Cultural Impacts
Archaeological Impacts
Transportation
LONG-TERM CONSIDERATIONS
Remedical Action Period
(Institutional Cootrol)
VOC Contaminant Removal
Radionudide Removal
30 years Not Applicable 30 years
No No No
Yes No Possibly, but unproven
Yes No Yes
Inorganic Contaminant Removal
EXPOSURE OP GENERAL PUBLIC
Construction
Routine
Negligible
Negligible
Negligible
None
Future Release Risk
Negligible
Negligible
Negligible
Accident
None
10".""''''''18.1...,..
.
~
-------
if~
li~
i!i
ifi
1(1
~
~
uf
.l: ,
. -
~~
.
~
TABLE 8-1-B
SUMMARY COMPARISON 011' POTENTIAL IMPACfS OF
PROPOSED ACTION AND ALTERNATIVES - ORGANIC TREATMENT
Impact Cat~lolJ Proposed Action Alternatives
Activated
Carbon Columna No Action UV Peroxide Oxide or Air Strippina
E~RONMENTALIMPACTS
Excavation Negligible None Negligible
Topographical Deformation (permanent) Treatment Facility None Treatment Facility
Endangerment Species Impact Negligible None Negligible
Wetlands Impact Negligible None Negligible
Cultural Impacts None N~ble None
Archaeological Impacts Negligible None Negligible
Transportation Umited None Umited
LONG-TERM CONSIDERATIONS
Remedial Action Period 30 years Not Applicable 30 years
(Institutional Control)
VOC Contaminant Removal Yes No Yes
Radionuclide Removal No No No
Inorganic Contaminant Removal No No No
EXPOSURE OF GENRAL PUBLIC
Construction Negligible None Negligible
Routine Negligible Future Release Risk Negligible
Accident Negligible None Negligible
-------
-------
SECTION 9
REFERENCES
l
.
Burney, 1989. Burney & Associates. Inc., An Archeological and Historical Survey of Selected Parcels WIthin
the Department of Energy, Rocky Flats Plant. North Jefferson County, Colorado, January 1989.
Cleveland, J.M., 1979, The Chemistry of Plutonium. American Nucl88l' SocIety, New York.
DOE. 1980. U. S. Oep&rtment of Energy. Final Environmental Impact Statement. Rocky Rats Plant Site.
Golden. Jefferson County. Colorado: U. S. Department of Energy ERDA 1545-0, DOE/EIS-0064, April
1980.
DOE, 1985. .Preamble: National Environmental Policy Acr. U.S. Department of Energy Order 544O.1C,
AprI9. 1985.
DOE, 1986, Comprehensive Environmental Assessment and Response Program Phase 1: Draft Installation
Assessment. Rocky Flats Plant; U. S. Department of Energy, unnumbered draft report.
DOE, 19888. U.S. Department of Energy; .Internal Dose Conversion Factors for Calc\Ntlon of Dose to the
Public., DOE/EH..oo71, Washington, D.C., July 1988.
DOE. 1988b. .Radlatlon Protection for Occupation Workers.. U.S. Department of Energy Order 54S0.11,
December 1988.
DOE, 1990b, .Radlatlon Protection of the Public and the Environment.. U.S. Department of Energy Order
5400.5. February 8, 1990.
DOE, 1991, .Federal Facllty Agreement and Consent Order/Inter-Agency Agreement.. U.S. Department of
Energy, January 22. 1991.
Donaldson, James C., and Logan MacMllan, 1980, .01 and Gas: History of Development and Principal Fields
in Colorado,. In Colorado Geoloav; HarTY C. Kent and Karen W. Porter, editors; Rocky Mountain
Associations Geologists, pp. 175-189
Dew Chemical Company, 1971, Anonymous Memorandum, January 15, 1971.
. DRCOG. 1989, "Pop IlAtion and Household Estimates.. Denver Regional CouneR of Governments, September
1989.
DRCOG. 1990, -oRCOG Reglonll Notes, 1990 Estimates", Denver Regional Counc. of Governments. July
1990.
EG&G. 1989, An AerIal Radlciogy Survey of the United States Department of Energy's Rocky Flats Plant:
Draft, Golden, Colorado.
EG&G, 199Oa, .Phase II RFI/RIFS WorkpIan, Final, Operable Unit No.2, 903 Pad, Mound and East Trenches
Area. AprIl, 1990.
EG&G, 1990b, "WeUands Assessment, Rocky Flats Site", prepared by Asi for EG&G, Lakewood, Colorado.
AprIl 1990.
SUFFACE WATER INTEI'IM AEMEOIAL AC'T1ON PI.NI
ROCKY FI..A TS PI..AHT. GOoDEN. CX)UJIWX)
eg&;._-,_ut,_.e......
_'99'
-------
EPA, 1985, CompIation of Air Pollutant Emission Factors. Volume I: Stationary Point and Area Sources,
PB86-124906. Research Park. Ne. September 1985.
EPA, 1988. U.S. Environmental Protection Agency. .Umltlng Valves of Radionuclide Intake and Air
eon..-lbcdU1 and Dose Conversion Factors for Inhalation, Submersion and Ingestion", EPA-520/1-88-
020, Washington. D.C.. September 1988. .
\
;
EPA, 1989. Risk Assessment Guidance For Superfund. Volume 1 Human Health Evaluation Manual (Part A),
EPA/540/1-89/002. December 1989.
.
EPA, 199Oa. -rechnology Evaluation Report: Site Program DemonstratIon of the Ultrox International Ultraviolet
Radiation/OxIdation Technology". EPA-540/5-89/012. CincinnatI. Ohio. January 1990.
EPA, 1990b, Health Effects Assessment Summary Tables. Fourth Quarter FY 1990. OERR 9200.6-303-(89-4),
October. 1990.
Gifford. FA. Jr.. 1961. Use of Routine Meteorological Observations For estimating Atmospheric Dispersion.
Nuclear Safety 2(4): 47-57. 1961.
Gifford. F.A. Jr.. 1976. Turbulent Diffusion - Type Schemes: A Review. Nuclear Safety 17(1): ~. February,
1976.
Hetzer. H.W., 1987, "ContInuous Upftow Fltratlon." American Water Works Association. Pennsylvania Sadion
Meeting. May 6. 1987.
Hurr, R.T.. 1976, Hydrology of a Nuclear-Processing Plant Site, Rocky Flats, Jefferson County, Colorado; U.S.
Geological Survey Open-Fie Report 76-268
IIIsley. e.T., 1978, Memorandum to M.V. Werkema. Rockwell International entlded .Briefing on Burial
Trenches.. December 19, 1978.
Ortandlnl, K.A, Penrose. W.R.. Harvey, B.R.. Lovett. M.B.. Findlay. M.W.. 1990. .CoIloidai Behavior of Actinides
In an Oligotrophic Lake, Environmental Science and Technology. Volume 24. No.5, 1990.
Post, P.. 1989. Personal Communication. U. S. D. A. Colorado Agrlc~raI StatIstics Service, November 1989.
Puis. R.W. and M.J. Barcelona. 1989, Ground-Water Sampling For Metals Analyses: EPA Superfund Ground-
Water Issue. EPA/540/4-89/0001
Rao, R.K, E.L Wlmot.-end R.E. Luna. 1982. .Non-Radlologicallmpact of Transporting Radioactive Materials,"
SAND 81-1703. TTC-0236. Albuquerque, NM. Sandia National Laboratories. 1982.
Robson, S.G.. J.e. Romero. and S. Zawistowski. 1981" Geologic Structure. Hydrology and Water Quality of
the Arapahoe Aquifer In the Denver Basin, Colorado: U.S. Geological Survey Atlas HA-647.
Robson, S.G., A Waclnskl, S. Zawlstowksl, and J.e. Romero, 1981 b. Geologic Structure. Hydrology, and Water
Quality of the Laramie Fox HUls Aquifer In the Denver BasIn. Colorado: U.S. Geological Survey
Hydrologic Atlas HA-650.
Rockwellintemational. 19878, Draft Remedial Investigation Report for 903 Pad. Mound. and East Trenches
Areas, U. S. Department of Energy. Rocky Flats Plant, Golden. Colorado. December 31. 1987.
Rockwellintemational, 1987b, Resource Conservation and Recovery Ad Part B - Operating Permit Application
for U.S. DOE Rocky Rats Plant, Hazardous and Radioactive Mixed Wastes, Revision 1: U.S. Department
of Energy. unnumbered report.
SURFACE WATEFI iNTER'oI REMECIAL AC'T1ON PI.AN
FIQCI(V ~\.AT$ "'..»IT. GOI..DEN. COLORADO
~.._,~....\_.e.....,
a..4atC:P'199'
-------
(
"
Rockwellintematlonal, 19888, Draft Remedial Investigation Plan for 903 Pad, Mound, East Trenches Areas.
Phase II Sampling Plan, U. S. Department of Energy, Rocky Flats Plant, Golden, Colorado, June 30,
1988.
ROCkwell International, 1988b, Draft Feasibility Study Report for High Priority Sites (881 HRlside Area),
March 1988.
...
Rockwell International. 1988c, Letter from George Campbell to Albert E. Whiteman, Rocky Flats Area Office
re: Endangered Species at the Rocky Flats Plant; J~y 15, 1988.
Rockwell International, 19898. Draft Interim Measures/Interim Remedial ActIon Plan and Decision Document
for 903 Pad, Mound, and East Trenches Area, U.S. Department of Energy, Rocky Flats Plant. Golden.
Colorado, December, 1989.
Rockwell International, 1989b, Quality Assurance/Quality Control Plan: Environmental Restoration Program.
- Roctcy Flats Plant, January 1989.
ROCkwelllntematlonal,1989c, Background Geochemical Characterization Report, U.S. Department of Energy,
Rocky Flats Plant. Golden, Cotorado, December 15, 1989.
Sax. N. I. and R. J. lewis, 1987, Hawley's Condensed Chemical Dictionary, Eleventh edition, Van Nostrand
Reinhold Company, New York.
Slade, D.H. (ad), 1968, Meteorology and Atomic Energy . 1968, TlD-24190, U.S. Atomic Energy
Commlssion/DMsion of Technlcallnformat/on.
Smith, R.E., 1975, Memorandum to D.J. Cockeram, Rockwellintematlonal, Rocky Flats Plant on Buried
Radioactive Material, September 2, 1975.
Sorg, T.J., 1987, ~evIew of Treatment Methods for Removal of Uranium from Drinking Water." AWWA Annual
Conference Seminar, Kansas CIty, Missouri, June 1987.
TIepeI, E.W., and J. Shorr, 1985, "Applications of Advanced Membrane Fltration to Industrial Wastewater
Treatment and Groundwater Clean-up, "Intematlona/ Water Conference, 46th Annual Meeting, November
4-7, 1985.
Weber, W.A., G. Kunkel, and L Sch~ 1974, A BotanicaIlnventcry of the Rocky Flats Atomic Energy
Commission Site, Final Report; University of Cotorado, Boulder, Colorado report COO-2371-2
SUFFACE WATER INTERIIoI ~ ACT10N P\AA
r:axY FI..A T9 F'\.AHT. GOU:IEN. CClOfW)O
~\_\-.ut\88C-4IJIW
MarCil' 99'
-------
~ . . ~~;~~- \~ .. ~ .
.. :..,.~",,:!-; .,.': c<~-.
." .,,,-,,,,,,,,f'~~;''''''''"c:.'ryC' "",'''X,",,,' CJ7. r~'~
- EPA ROD) R Of; - 91 )OS
-------
':~.~~.:~~~:~'-:-~~ .
. -
..,.
. '~'.~?~ .:..'
DOEjEA - 0496
SURFACE WATER INTERIM MEASURES/INTERIM REMEDIAL ACTION PLAN/
ENVIRONMENTAL ASSESSMENT AND DECISION DOCUMENT
SOUTH WALNUT CREEK BASIN
OPERABLE UNIT NO.2
VOLUME II
U.S. Department of Energy
R~ FI8ts Plant
Golden, Colorado
8 MARCH 1991
FINAL
Prepared by:
EG&G Rocky Flats, Inc.
Rocky Flats Plant
Golden, Colorado 80401
REVIEWED FOR CL~SS:F;C.~TfON/UCNI
By F. J. C:!r~::~
Date 3 - 2-2 -7 I
-------
-------
.
.
. ,
~,
SJI'!I'ACE WA"!'E"' 1"'-:-EI'!IIwI REIwIEOIA~ AC"'lON P\.AN
..X"" =~~5 """''''-. GO:.!>EN. CO..OClAOC
.;'-; ,-t:a:: waJlO'I..r acoe"'C:.:Jgs
APPENDIX A
DATA TABLES
OPERABLE UNIT NO.2
-------
. ~;~... ..
TAIlE A-1
uacGllOl8 _-"TEl (SEalit _10 ,.)
TCl.O-- 8MEIVA&. Wfift ulens
.. ....1- .TECTID ValUE
Rocky
flet. VeUey flU Weethered Welthered &hMlthered
AII""IUI CoU""IUI AII""IUI Cllptone '''''tone ,""tone
Anelyt. ....1 t. (11 5...,Iea) (2 5...,1..) (8 S8llple.) (4 5811p1..) (2 S8IIp1..) C7 SlIIIpl..)
Dissolved "etlls
AhalfUII 118/1 ... lit ... ... ... 0.527*
Antl~ 81'1 ... lit ... lit ... ...
Arsenic II!J I I ... ... ... ... ... 0.0186*
Bart UII 118'1 '" lit ... lit ... ...
BeryiliUl 1119/1 NO 110 110 110 NO ...
ClKhh.n 1119/1 NO 110 NO NO NO ...
Calcha 1119/1 85 76.8* 138 13.4* 65.1* 64.6
CeslUil 1119/1 NO 110 ... NO lID lID
ChrOlllhn 118/1 NO NO ... lID 0.0122* '"
Cabel t II!J' I ... NO ... ... lID ...
Copper 118/1 lID lit lit lit ... lit
Iron 118,1 0.266* lit 0."* lit NO ...
lead 118/1 NO lit NO NO lID NO
LlthlUl 81/1 '" 0.172* 0.028 .011* 0.0106* ...
HagneslUl 118/1 5.19" 15.3* 26.57 45.3* 9.41* ...
Hang-.. III' I 0.365 0.088* 0.686* 0.126* 0.292* 0.0182*
Mercury 118/1 NO NO 0.003* .0088 lID lID
Mol ytxIent8 118'1 0.0136* lit lID 0.015* 0.015* 0.112*
Nlchl 118'1 0.0432* NO ... NO ... ...
PotesslUil II!J II 7.13* 110 ... ... ... 21.89*
SelenlUl 1111 I NO NO 0.0114* NO ... 0.041*
Sit ver 1111 I lID 110 NO NO NO lID
SodlUil II1II/1 13.4 98.1* 88 36.9* 25.6* 599
StrontiUl II1II/1 0.159* lit NO NO ... 0.451*
Ihall iUl 118/1 lID NO NO 0.01* ... NO
Iin 1119/1 '" NO NO NO ...
vanadhn II1II/1 NO NO NO NO ... NO
Zinc 1119/1 0.11,1* NO 0.0212* 0.101* ... 0.564
eg&g\sw-irap\tables\tbl-e-'.
-------
'H .-
.
.
,AIlE A-I (cont.)
IA£l(G1MU8 ---..." (SEa8 ...m 19IW)
'fill D~ .IIUnAl UftII LlRns
.. ...l1li DEfEctED VAlUE
Rocky
fletl Ve"ey fill Weethered Weethered lhMeth.red
AIIlNh.. tollwlUl AIIINIUI Clere'one s""tone ..-tone
ANllyI' Urd.. (11 58lllP1el) (2 5..188) (8 58IIIPI.I) (4 58lllP1es) (2 58111P188) (7 S8IIIPI.s)
Other
Tot II Dllsolved Solids ..'I 352 520* 947 320* 170* 1761
Cerbonete ..II lID .. .. .. .. 49
81eerbonete ..'I 436 '10* 719 400* 140* U2
Chtorlde 1811/1 15.6 20* 40.29' 11* 15* 607
Sulfate 1811' I 45.1 86* 150 "* 16* 950
Nitnte 1811/1 2.98 0.18* 0.69* 0.58* 1.6* 0.610
Cyenlde 1811' I .0038* lID lID 0.0036* lID lID
pM 8.6 (5.98) 7.4* (7.1)" 8.61 (6.12) 8.2* (7.4)** 7.5* (7.2)" 10.57 (7.43)
Oillotved Redlonuclldes
Gross Atpha pCl,l 12.543 27* 13.515 12* 7* 13*
GrOll lete pCllI 14.570 12* 18.530 7* 2* 15*
Ur....IUI 2n, 234 pCI,I 1.647 11* 6.481 5.8* 1.1* 12.936
UranlUil 2U pCI,I 0.000 0.3* 0.232 0.2* 0* 0.135
Ur8l'llUil 238 pCl/I 0.195 7.7* 5.084 3.2 0.6* ].3507
Strontltll 89, 90 pCl,l 0.552 0.1* 0.878 0.1 -0.1* 0.2*
Ptutonltll 239, 240 pCl,l 0.009 0* 0.012 0.03 0.01* 0.000
Amerlcltll 241 pCt" 0.000 0* 0.012 0 0.01* 0.019
CeslUil 137 pCl,t 0.603 0.2* 0.776 0.4 0.]* 0.7*
Trltitn pCl,l 309 100* 505 100 100* 731
. ...111- Detected Vatue
.. "Inl- Detected Vatue
NO Mot Detected at Contract Required Detection Li.it
() 'olerance Internet Lower LI.lt for Two-Sided Par...ter
-------
I.~ ..
1A1lE "-2
IAClCG11C118 _fM:E ""EI (s(a8 _TlI 1989)
nJllpa8'8 IIRDVAL II'f'R lU.ITS
.. ...1l1li DETICTED VALlE
lound 1 (7 l..pl.I)--
Anllyte Unltl 10t,1 Dtllohed
"etels
AIUlI.... l1li1 I 0.916- 0.485-
Antl80RY l1li1 I ... ...
Anenlc l1li1 I ... ...
larlUl l1li11 "' '''
Beryl I IUI l1li1 I ... ...
C_IUI l1li1 I ... ...
C.lclUi III' I 85.01 85.92
CeslUl 111/1 1.00- II)
Chr08lh.. 111'1 '" II)
Cobil t 111/1 '" II)
Copper l1li11 '" II)
Iran l1li11 '.17 1.78-
hid 111/1 '" 0.006-
UthlUl l1li1 I ... ...
",gnnIUl 1liiI' 12.48 12.82
"'"IIIMle l1li11 0.636 0.368-
Mercury l1li1 I 0.001 0.001
"olybdetul l1li1 I ... II)
,.. ckel l1li/' ''' II)
Pot...IUI l1li/' ''' II)
SelenlUl l1li/' ''' II)
5 II Iter l1li1 I 0.001. ...
SodlUl l1li1 I 47.36 46.22
Strant IUI 1liiI' 0.S82 0.40
1h.1 I IUI l1li/' ''' II)
1In III" '" lID
V8n8dhn 111'1 II) lID
llnc 1119' I 0.027 0.032*
eg&g\sw-irep\tebles\tbl-e-2.
.
-------
. ~;~ ...
.
.
TMlE A-l (cant.)
uac..... .,Am IM'fBI (SEa8 8IIIII'fBI 198P»
ftJlH8:E '11O¥M Wft1t u..n.
.. ...1181 _RCTID VAllE
"l18lyte
Unlu
lound 1 (7 l-.pl..)..
Tot.I Diliolved
Other
Totll Dlesolved Solidi
Carbanlte
If urbanite
Chloride
Sulfate
Nitrate
Cyanide
pH
111/1
111/1
111/1
111/1
111/1
1111 I
1111 I
271. 16
..
296.97
106.9
48.82
2.69
..
8.69 (6.60)
ItA
NA
NA
NA
NA
NA
NA
NA
lIadlcnJCI fdes
Groll Alpha
GrOle let.
UranlUl 2]). 234
UranlUl 235
UranlUl 238
StrontlUl 89. 90
PlutonlUl 259, 240
MertciUl 241
CesiUl 137
Trlt h..
pClII
pCl/'
pClII
pCl/'
pCl/'
pCI/I
pCI/I
pCI/I
ptl/l
pCI/I
7.74
9.89
1.45
o. In
0.805
2.04
0.018
0.042
0.599
258
4.38
8.80
1.40
0.133
0.957
1.398
lID
0.013
0.412
"A
""
lID
()
.
..
Not "nelyzed
Not Detected
Tolerence tntervel Lower li.lt for Two.Sided 'er8leter
""11- Detected Value
At Stations 5\1-104 end 511-80, 80st total end a few dissolved conatltuents were unc:heracterlaUcany high relative to the other data.
To be conservative. these dete ere not included in c~tatlon of the tolerlnce Interval.
-------
TAILE .-3
-- IEDIIEIIT
TOI.P'- IMTElYAL IJIIIB u.ns
C8 UXI- DE1KfB VALlE
.
FE8UUT ,.
...r .
L iait
ANlyte ~its C9 I811pl..)
Totll ...tlll
A hai NIl l1li"1 24719
Ant iaany l1li"1 lID
Ar'88ftic l1li"1 '3.0-
larha l1li"1 '128
laryll ha l1li"1 lID
c.a.i 'iI l1li"1 ND
C8lci'il IIIIki 72551
C..i'il 111/"1 lID
eta...i 'iI III/ki 43.38
COb8l t ../"1 lID
Copper l1li"8 22.0-
Iron 8IIk8 2IS08
L8Id ../"1 39.502
., Lithi'il l1li"8 lID
~,
...... i 'iI l1li"1 4110-
~ IIIIk8 372.20
I88rcury l1li"1 lID
_l yt8n.a l1li"8 lID
Mickel l1li"1 29.9*
Pot... i'il IIIIki lID
leleni'il l1li"1 lID
Silver l1li"1 6.r
SOdi 'iI 811"1 lID
Stronti'il ,,/k8 175*
Thalli~ "/''8 NO
Tin III/k8 NO
V8Ndi~ 111;/"8 50.2.
Zinc IIIII/k8 92.688
-------
TAILE A-3 Ccant.)
.----- IBUIEIT
TO! ElUC! IIITIIVAL IIftI UKITS
ca MlI- IIETEC'IBI VALlE
.
FE8IMIY ,.
. Upper
L 181 t
ANtyte unln C9 Sllllpt..)
SWE
Iltrlte IIIIkg II)
pi! 9.CB Ca. 77)
ToUI R8dloru:lldel
GI'088 A 111M pCI/SIII 60
Grou leu pCl/SIII 50
UI'8ft". Z33. 234 pCl/SIII 1.669
UI'8ft". as pCl/SIII 0.176
Ur8'l". 238 pCI/SIII 1.755
Strant h. 89, 90 pCl/SIII 1.390
Phrton". 239. 2100 pCI/SIII 0.096
;t A88rlc". 241 pCI/IID 0.029
C81h. 137 pCl/SIII 1.578
Trlth. pCl/8L 0.401
II) lot Oetected
. ....1- Oetected value
() Toter8'IC8 I nterve I Lowr L i.1 t for Two.Sided
Par_tar
-------
~.~ . w
IMlE A-4
IMXIIICI8 GEOlOGIC ..nl.AlS
leU891'S 181f1VAl 8I'ftI URns
.. MI.IIII DEIECftD VAllE
1.,
loclty
fI.t. We.thered We.thered
Allwh.. CollwlUl CI.yatone ,"'tone
Anelyte Units (70 SlIIplea) (28 SlIIples) (17 SlIIpl..) (4 SMpl.a)
Tot.I Metals
Alu.inua .../ltg 25312 2166] 13495 10300*
Anti80RY .../ltg II» II» 16.2* II»
. Arsenic IIII/ltg 15.86 7.7 15.05 ].6*
BariUl IIII/ltg 155.8 345.8 240.1 165*
Beryl I iUl l1li1 kg 11.27 17.75 11.8 2.2*
CedlliUl I119/l1g ].2* 1.8* NO NO
Calc iUl IIII/lIg 43079 20811 1018] 5940*
eesit.. IIII/lIg II» 274* II» lID
ChrOllh.. IIII/lIg ]1.9 26.8 16.57 10.18
Cabelt IIII/lIg 18.2* 15.9* 29.7* 20.5-
copper IIII/lIg 20.0] 26.7 SO.62 19.6*
Iron IIII/kg 22916 29991 41295 12]00*
Lead IIII/kg 18.04 26.4 ]4.5 1].4*
Li thiUl IIII/ltg 44.4 ]l.1 ]].]1 7.0*
MagneslUl IIII/ltg 4425 6151 4896 2520*
Mengene.e IIII/kg 422.9 545.1 656 ]05*
Mercury IIII/ltg 0.58* 0.44* 0.]5* 0.27*
Mol ybdenI8 IIII/ltg ]8.65 ]2.78 ]].68 11.2*
lIiellei IIII/ltg 4].27 ]5.4 56.95 14.]*
pot..aiUl l1li1 kg ]]]6 2789 1400* II»
SelenlUl IIII/ltg II» II» II» II»
Silver IIII/lIg 40.9* ]].5* 18.18 12.18
SodlUl IIII/kg II» ]680* : II» II»
StrontiUl IIII/ltg 226* 111.1 144.42 69.2*
Ihalt IUI l1li1 kg II» NO ' II» II»
IIn IIII/ltg ]]8* 441* 214* 268*
vanediun 11191 kg 54.67 58.2 47.7 22.2*
Zinc I119/l1g 52.64 98.1 . 106.7 79.9*
eg&g\sw-irap\tables\tbl-a-4.
.
-------
. ~.; .-
c,
.
'AIlE A-4 (cont.)
1MaWN- ClfOlCIGIC MIOIAlI
1111 BI~ .lmMIL II'ft1t URns
.. ....1.... DEtfC1tD VAllE
1989
Rocky
FlaU Weathered W.athered
Allwl... Collwl... CI-vatone I8ndItone
Anelyte 1)\ It. (70 S..I..) (ZI 1..1..) (17 $..1..) (4 ...1..)
2!!!!.t
Sui f Ide lII,kg 13. 5. 5. 2*
II it rete lII,kg 4.5. 4.274 2.08 1."
pH 9.64 (6.06) 9.48 (6.96) 10.14 (7.04) 9.28 (8.0»-
lotal Radlonucll~
Gross Alpha pC 1'111 57.108 51.710 52.502 37
GrOll let a pC 1'111 36.886 55. 135 55.745 29
Uranl... 255, 254 pC 1'111 1.491 1.759 1.985 0.8
uranl... 255 pC 1'111 0.087 0.169 0.258 0.1
UranlUil 2J8 pC 1'111 1.555 1.675 1.645 1.0
StrontlUil 89, 90 pCl'lII 0.768 0.776 0.786 0.4
PlutonlUil 259, 240 pC 1'111 0.017 0.025 0.020 0.01
Allerl c"", 241 pC 1/111 0.018 ... IIR ...
Cesl... 137 pCl/gIII 0.082 0.113 ... 0.0
IritlUII pCl,.1 0.410 0.299 0.522 0.39
()
Not Detected
Data lIot Received
Maxl.u. Detected Value
Minl.u. Oetected Value
Tolerance Interval Lower LI.lt
for Two-Sided Par...ter
NO
IIR
.
..
-------
. 4~.- .
fAllE A-S
VOlAJiLE CIICAII.C aJIIIOIIItI DEfECtED ..
....,... -- ..lEI
IE"" ...IEI 1989
Cerbon letre- 1,1-01- 1,1-01- lotel-1,2-
letre' dI I oro' Irlchloro- eM oro- Methylene Chi oro- a.loro- Vinyl Certlan Dlchloro.
D8te chloride ethene 8th... fOl"8 Chloride 8th.. .th... Chloride Ac.tane Dlautflde .theM loluene
!!!tt.1a Hill ~ (UIII n ..!YIlU.. (UII/I) 1!!IlU (Ull/I) .JYIlU. .JYIlU. (UII/ n .JYIlll. (UII") fUll/I) .JYIlU.
Rocky 33-86 5/04/89 Dry
flet. 39-86 5/08/89
AlluvlUl 41-86 5/10/89
42-86 5/08/89 1,100 300 190 21J
45-86 5/04/89 Dry
10-87 5/02/89 Dry
15-87 5/01/89 1,100J 190 120 21 5J
17-87 5/03/89 47J 1601 17 4J
19-87 5/04/89 Dry
24-87 5/09/89 Dry
26-87 5/09/89 Dry
27-87 5/10/89 15 31 4J 3J
32-87 5/09/89 Dry
]]-87 5/09/89 Dry
3S-87 5/09/89 Dry
ColluvlUl 63-86 4/13/89 Dry
67-86 5/09/89 Dry
29-87 4/24/89
104-87 4/13/89 Dry
Velley 35-86 5/03/89 11 59 13 470 ]J
flit )6-86 5/04189
Alluviun 37-86 5/0]/89 ]OR
64-86 5/31/89 8J
65-86 4/13/89 2J
66-86 6/02/89 26 1J 3J
21-87 5/03/89
o,I,\o_-lrop\tbl-o-5.
~
-------
I,,~ . - ~
.
\oJ
,AIlE A-5 (cant.)
VOlAIiLE CIIGAIIIC ~s DE'ECtED I.
uallfllED .... "I(I
SEa8 ""EI 19tW
Carbon letr.- 1,1-01- 1,1-01. 'otal.I,2-
tetra' ehloro' Irlehloro- Chi oro. ...tllyl- eIIloro. CII I oro. Vinyl carbon Olcltloro.
Date ellioride ethene ethene fo... Cltlorlde ethane et,*- Cltlorlde Acetone Dlaulflde etllene lol'*-
"etrlx Hill b!I!1.!5I (ugJ I) .J.!BlU... (ua/I) 1YIlU (uaJ I) -Ylll. -iYIlU.. (ua/I) -WI61. (ua! I) (uaJI) -iYIl11..
\leethered 1-71 5/01/89 690J 69 230 200 5J
Claystone 2-71 5/01/89 8 440 7 8
1-74 5/03/89 45,000 1,800
3-14 5/08/89 1,100 50 25 11J
Ueethered 62-86 4/11189 2JI
sends tone 9-81 5/01/89
11-81 5/02189 Dry
12-81 5/02189 Dry
14-87 4/24/89 160J 4J 68 16
23-81 5/03/89 74.
25-81 5/08/89 290 840 120 5J
]6-81 5/08/89 610 350E 12,000 290E 22J 2J
J -
E
II
8 -
Velue estl_ted below detection II.tt
Velue .atl_ted
Velue rejected by data yal idat ion
CoqJOlRt allo detected In assocl.ted blank.
-------
H'.
U8U A-.
voumu OROANIC COMPOUND. DnECUD
IN ~UND WA''''
...A-IIM cONCnlllAno".'
Carbon '.tr... 1.1-01- I. 1-01- Tohl-1.2-
'.tr.- ch1oro- Trlc.,loro- ChI oro- Chloro- Vinyl C.rbon Otct'l1oro-
chlortde' .th_n- .then. Chloro. "",I"yl.n. .then. .then. Ch lorld. Aceton8 Ohul fld. et-
~ !!ill ( Uq/ II J.!!aL!l luq/11 ~ Chlorld. .1!!sL!L .1!!sL!L ...1!!sL!L ...1!!sL!L lUll/II ( Utl/ II
Roc.y ]]-86 Dry
r I At, 39-86 845 418
Alluvium 41-86 160 JJ8 6J8 17 7
42-86 4835 J200 1400 107 J20 26 5J t7
U-86 6 8
10-87 Dry
15-87 4305 900 510 42 5J 13008
11-87 OJ 160R 8J 4J 15 9J8
19-87 Ory
2.-87 Dry 19J8
26.87 Dry 5J8 31
21.87 15 44 4J 3J 3J8
32-87 95 44 2J8 H 6J8
H-87 Dry
35-87 Dry
Colluvium 6)-86 Dry
67-86 Dry
29.87 99 4J 268 9J8
44-87 Dry
Vo II.y f t I I 35-86 12 19 340 36 62 48 930 1600
Alluvium J6-86 6
37-86 JOR
6.-86 8J
65-86 8 2J .JJ
66.86 26 23 3J
21-87 49
W..thered 1.71 4800 800 2000 1525 14 535 5J 346
(1.y,ton. 2-71 40 8 28800 410 12 28 10 92
1.74 528000 18000 38 5J 20 90 6J8 15
3-74 1885 1080 812 45 56J 22 84J8 15
W..th.red 62-86 2J 2JI
S8ndttone 9-87 10 7J8
1\-87 605 28 1090 129 4J
12-87 58 57 3570 17 9
14-87 404 4J 109 23 7 IJ 21
23-87 74R 4J8 3J8 8 3J8
25-87 835 840 258 6J8 UJ8 1108
J6-87 )673 4654 221860 5427 119 1044 38
....'
f4
-------
!!!!!J.! ~
Roc. y 33-86
r fat, 39-86
Alluvtum 41-86
42-86
4J-86
10-87
15-87
17-87
19-87
24-87
26-87
27 -87
J2-87
n-87
35-87
(olluvlum 63-86
67-86
29-87
44-87
VoII.y r" I J5-86
Alluvium 36-86
37-86
64-86
65-86
66-86
21-87
\I..th.red 1-71
(18.,Iton. 2-71
1-74
3-74
"'..th.red 62-86
Cj,andston8 9-87
11-87
12-87
14-87
23-87
25-87
36-87
............-......
To'uen.
i!!aL!L
1.2-01-
Chi oro-
.the".
.l!!sL!L
1.1.1-
'rl-
Chloro-
.th.n.
.l!!sL!L
4J8
12
JJ8
56
32
400 2892
24 47
16
22
301
1472
. J,;~ .-
..
.
IMLI A..lconl.'
\IOI.A'IIU OMAIIIC COMPO"". "'KIm
III "'''''0 WAIBI
MA- CONCIN""'noN8'
2.h...-
non8
i!!sL!L
-------
J' .M
..,
'.LI "'.fcon.'
vaunu CIIIIIANIC COMPOUIUJe 1In1e'.
.. _UNO WA'"
M.- COIICIIW11UITfOII8'
J
(
R
8
Ooto obto'nod 'rom tho 1987, 1988. 1989 'fold 'nvootfgotlono
A carbon tetrach10rtda concantratton ya1u. of 2292 ppb .a. raported for We" No. 39.86 (4 Hay 1988). 'hi. datum I. .u.pact due to prob1... ob.arvad In tha ana1yt'c81 laboratory
tha "r.t hal' of 1988. A11 othar ground-water concantratton data obta'ned 'ro. tha 1987, 1988, and 1989 "ald Inya.tlg8tlon. (9 data point.) .how "non-datect" concantratlon
for corbon totrochlorldo ot Wol' No. 39-86.
Velue e.tt~.ted below datectlon 1t~lt
Valua a.tlm.tad
Va1u. rejected by data va"datlon
Compound ."0 detectad In ...oclatad b1.nk
during
va1u..
...".-
.
-------
TABLE A-7
INORGANICS ABOVE BACKGROUND IN GROUND WATER1
.
Number of Range of
RIIUts Background MaxImum
. Abr:Ne Number of Corw~adonJ Cancermatlon-
Analyte BackgroundZ Results (mg/l) (mg/l)
Bicarbonate 45 257 140-719 530
CNoride 172 257 11 «)7 819
Cyanide 0 62 ND-O.038 ND
Nitrate 164 255 0.18-2.98 15.5
S~e 114 257 16-950 1157
Total Dissdved Solids 193 257 170-1761 3219
. ,
.;.,..
ND
Not detected at contract required detection limit
Concentration data obtained from the 1987. 1988. and 1989 field Investigations.
z
J
Compared to background value for appropriate lithologies. listed in Table A-1.
Range of maximum values for different classes of ground water.
-
Reponed when maximum concentration is above background.
-------
TABLE A-8
DISSOLVED METALS ABOVE BACKGROUND IN GROUND WATER1
.
Number Of Range of
RIIUts Background Maximum
AbrNe Number of ConcentratiOn3 Concentration'
AnaIyte BackgroundZ Results (mg/l) (mg/l) .
Aluminum 119 253 ND-O.327 4.75
AntImony 18 248 ND-NO 0.12
Ar8enic 9 247 NO-o.0188 ., 0.007'
- Barium 215 253 ND-NO 0.83
Cldmlum 1 249 ND-NO 0.006
Calcium 161 253 64.6-138 408
Cesium 0 248 ND-NO NO
Chromium 54 253 No..o.0122 0.1223
Copper 93 253 ND-NO 0.84
Iron 131 253 ND-O.94 4.35
l8d 15 247 ND-NO 0.04
., UthIum 7 eo ND-O.172 0.22
-
Magnesium 164 253 ND-45.3 136
Manganese 103 253 0.0182-0.686 4.37
Mercury 1 245 ND-O.OO8 0.013
Molybdenum 41 253 ND-O.112 0.192
Nickel 51 253 ND-O.0432 1.7
Potassium 92 245 ND-21.89 44.5
Selenium 39 246 ND-O.091 0.39
Siver 7 253 NO-NO 0.13
Sodium 117 253 25.6-599 405
Strontium 266 253 ND-O.451 7.7
Thallium 0 240 No..o.01 0.01
Vanadium 9 253 NO.NO 0.10
Zinc 65 253 ND-O.564 2.70
ND
Not detected at contract required detection limit.
Concemration data obtained from the 1987. 1988. and 1989 field investigations.
Z
3
Compared to background value for appropriate lithologies. listed in Table A-1.
Range of maximum values for dlfferem classes of ground water.
.
Reported when maximum concemration is above background.
-------
TABLE A.I
DISSOLVED AADIONUCUDES ABOVE BACKGROUND IN GROUND WATER1
..
.
AnItyte
Number of
RaUb
Abt:N8
Background2
Number of
Resutts
Range of
Background
ConcentratIonJ
(mg/l)
Maximum
Cor- ~dtion.
(mg/l)
Gross Alpha 42 179 7-27 250
Gross Beta 46 180 2-18.53 -872-
Uranium 233,234 62 151 1.1-12.94 34
Uranium 235 62 148 ~.232 1.7
Uranium 238 73 151 0.6-7.7 28
StrontIum 89.90 3 153 0.1-0.878 5.0
Plutonium 239. 240 3 153 ~.012 0.52
Americium 241 6 153 ~.019 0.83
CesIum 137 0 3 0.2.Q.776 0.3
.,
...;
2
Concentration data obtained from the 1987. 1988. and 1989 field investigations.
Compared to background value for appropriate tlthologies. listed in Table A-1.
J
Range of maximum values for different classes of ground water.
Reponed when maximum concentration is above background.
.
-------
~.~ .~
'MLE A.10
VOLA'fIlI ~ COMPOUIIID8 Dnu:,m IN _La'
Tote 1
I. I -01- 1,1-01- 1.2.01 1,2-01-
Vln,l C"'oro- "'lh,lene Carbon Chloro- Chloro- Chloro- Chloro- Chloro..
lorehol. Chloride (thene Chloride Acetone Ohu1flde [thene [thene [then. Fa..... [thane 2.8utlnon.
~ 1!!ill..IL iI!illsl ..1!!al!.9.l 1!!sful (Ug/kg) 1!!sful i!W!JIl. 1!!sful !i!illIL i!W!JIl. (ug'h)
90.1 Pod - 8H2281 48J8
Roc"~ f1at, 8H2.181 6J 1208
Alluvtum 8H2981 IIJ 4108
8H.1081 .11.68 2.108 )JJ
90) Pad - 8H2481 41.18
Colluvium 8H2587 7J 46.98 II 008 210J
8H2681 208 2.1
8H2187 7J 1408
8H2887 12J 708 I7J
90J Pad - 8H2987 10J 4108
Sandstone
QO.1 Pad - 8H2281 9J 788
(18~,ton. 8H2)87 9J 1508
8H2481 198 608
8H2587 150J8 11008 IJOJ 150J
8H2687 8J 120
8H2787 6J 1708
8H2887 IIJ8 58
8H)087 9J 2008 16J
Mound - Rock, 8H.1181 I7J 100 32 6J
f 18t, Alluvtum 8H.1287 9J 120 29
8H.1.187 190
8H.1487 500
8H )587 ~
8H.1687 IIJ 5)
8H)187 .17.4 48J8
8H.1887 12J 1208
Mound. 8H.1.187 15J .120 10J
S.nd.ton. 8H.1487 1.10
Hound. 8H.1I87 9J 110 ~J
(Ia~'to"e 8H.1287 170 19J
8H.1587 280
8H.1687 8J 6.
8HJ787 17J8 1508
r..t trench.. 8H.1987 220 1'0
Aoc., fl.t. 8H4087 140
Al1uvturn 8H4187 210
8H4287 71
8H4187 20J .160 150
8H4487 IIJ 1608
8H4587
8H4687 5J 2108
g\_Ir8P\tebln\tbl..\O.
.
-------
J...~ . ~
.
"
'Alill 11.10 Cconn
votAnlI 0MAMc: COM",- DOIIe'ID", 8OtU'
Tote I
1.1-01- 1.1-01- 1,2-01 1,2-01-
VInyl Chloro- Methylene (.rbolt ["10ro- Chloro- Chloro- Chloro- Chloro-
80r.ho1. ChlorIde (thene ChlorIde Acetone Ohulflde (thene Ithan- Hhene Fono Ethene 2-8utenone
~ .L!!ailiL 1!W..W lugHg) i!!B..l!..il lug/kg) .L!!ailiL i!!.ILW i.!!..sllil i.!!..sllil .Lgful lug/kg)
£.,t french., IH4787 7J 8201 1401 21J
Aoc~y '1.t, IH41187 III 2201 8J
Alluvium IH4987 7JI 7101 2JJ
IH5087 10008
8H5187 6J8 17008 24J
8H5287 U8 518 7J
8H5J87 IIJ 20008 JO
8H5481 141J8 16008 120
8H5587 8J8 12008 100
8H5681 48 1208
[",t french., 8HJ987 140 58
Send_ton. 8H.287 140 6J
8H4487 1808
8H4587
8H5181 6J8 128 8J
8H5687 Z6 1108
[.,t fr.nch., 8HJ987 12
C hy,ton. 8H.081
8H. 181 1J
8H4J81 210 180
8H4587
8H.687 7J 2108
8H4187 12J8 1108 100
8H.1I87 IZ008
8H4981 7J8 1208 J4
8H5081 10008 110
8H5281 15J8 948 26
8H5J81 9J8 24008 IU
8H5481 15J8 4608 20J
8H5581 8J8 6208 78
8H5187 368 2608 10J 100
-------
901 Pod-
Roc.y fl.t,
A11uvtum
90] Pad.
Colluvtum
903 Pod -
Sandtton.
90J Pod -
( 18Ylton8
Mound - Rocky
rt8t~ Alluvtum
Mound -
Send.tone
Hound -
(18)'Ito"8
E.,t french..
Rody f lots
Alluvtum
Borehol.
!!!!!!!!!!.!:
8H2287
8H2387
8H2987
8HJ087
8H2487
8H2587
8H2687
8H2787
8H2887
. 8H2987
8H2287
8H2387
8H2487
8H2587
8H2687
8H2787
8H2887
8H3087
8HJJ87
8HJ287
8HJJ87
8HJ487
8HJ587
8HJ687
8HJ787
8HJ887
8HJJ87
8H]487
8H )\87
8H]287
8HJ587
8H]687
8HJ787
8H]987
8H4087
8H4187
8H4287
8H4]87
8HU87
8H4587
8H4687
g\_IrIOp\labln\lbh. I O.
""I-Trl-
Ch'oro-
Ethana
IUII/kgl
5J
C.rbon
Y.t,..-
Chlorlda
~
100
~ ..
T Mll 11.10 Cconl.1
\IOU"'''' OMANIC COMPOUNDS MTI'CTm... 801L8'
1,1,2,2-
Trl- 1.1,2- ,.t,... Tatra- I, ]-DI-
Chloro- Trtch'ot'o- Ch10,"0- Chloro- Ethyl Total Chloro-
Ethona Ethana Ethana Ethana Toluene 18".18"8 Strr8n8 .,'anu Prop.n.
.1!!.UW Iug/kgl 1!!sfuL -1J!aLW 1J!JI.l!sL 1!!.IL.W 1!!.IL.W 1!!.Ii!.I.1. 1!!.IL.W
17J
7000
10000
640
780
3]00
15J
84
180J 16000 ]800 ]]0 290 480
5J IU 6J
20J 7J
7J
7J
6J
1]0
190
125
.
-------
£..t french..
Aor..y rt.t.
At luvtum
r.,t frenche.
Send.tone
(.,t frenche,
[1.yston.
Borehole
~
1.1. 1- Ir 1-
Chloro-
Ethana
lu.".1
Cerbon
Tetra-
Chlorlda
lu."..1
~.~ ...
.
Ii
BHHB7
BH4B87
BH49B7
BH50B7
8H5187
8H5287
8H5J87
8H5487
8H5587
8H5687
IJJ
'Ull 11.10 Icon...
YOU"'''' ~ COMPOU1M18 DOIC'&» IN 10118'
1.1.2.2-
'rl- 1.1.2- '.tr.- ,.tr8- 1. )-01-
Chloro- trtch'oro.. Chloro- Chloro- Eth)'1 10\81 Chloro-
(th8n. Ethana Et han. Ethana 'ol".ne 18.,.8n8 Styre.,e .)'I.n.. Prop.ne
.1!!JLl!al lud,..1 .1!!JLl!al ...iJ!aL.!!.al .1!!JLl!al .I.!!aL!al J.9ilil 1!!JILW. J.uL!!sL
)4
21J
150
27
62
25
8H)9B7
8H4287
BHU87
8H4587
BH5187
BH5687
BH]987
BH40B7
BH4187
BH4J87
BH45B7
BH4687
BH4787
BH4B87
BH49B7
8H50B7
8H5287
8H5)87
8H5487
8H5587
8H5787
180
110
8 - Compound .1'0 detected tn ..,oct.ted bl&h~ V.lue .,tt~ted below detect ton Ifmtt
Concentratton data obtatned 'r~ 1987, 1988 and 1989 field tnve.ttgatton,
-------
TABLE A.11
SEMI-VOLATILE ORGANIC COMPOUNDS DETECTED IN SOlLS1
.
bIs (2-
N-N1troso- dl-n-Butyl EthyIhexyI)
Borehole phenylamlne Phthalate Phthalate
Number l.a/ka\ l.a Ika\ l.a/ka\
903 Pad Rocky Flats Alluvium: 820
BH2287 35J 97J
BH2387 2300
BH2987 840B
BH3087
3400 3100
903 Pad Colluvium:
BH2487 36J 690J 3300B
BH2587 63J 1900B
BH2687 15QJ 4200J
BH2787 340
BH2887 51J 61J 3400
903 Pad Sandstone:
BH2987
.,
~,
903 Pad Claystone:
BH2287 89J
BH2387
BH2487 640B 2600B
BH2587 56J 830B
BH2687 160J 800
BH2787 220J
BH2887 2100
BH3087 1800B
Mound Rocky Rats Alluvium:
BH3187 490
BH3287 310J
BH3387 530
BH3487 50J 450
BH3587 92J 680
BH3687 83J 480
BH3787 170J 8700B
BH3887 73J 4600
Mound Sandstone:
BH3387 450
BH3487 35J 220J
Mound Claystone:
BH3187 40J 430
BH3287 9J
BH3587 320J
BH3687 38J 360
BH3787 41J 550
Concentration data obtained from the 1987 field investigations concentrations reflect maximum
values for the stated borehole.
-------
TABLE A-11 (continued)
SEMI-VOLATILE ORGANIC COMPOUNDS DETECTED IN SOILS
..
bIs (2-
N-NJtroso. di-n-BUtyt EthylhexyI)
Borehole phenylamine Phthalate Phthalate
. Number (itetlko\ (ao/ko\ (ao/ko\
East Trenches Rocky Flats AlILNium:
BH3987 33J 38)
BH4087 280J
BH4187 380
BH4287 170J 500
BH4387 49.1 830
BH4487 40JB 380B
BH4587 880
BH4687 250J
BH4787 120JB 260JB 1000B
BH4887 42JB 670B
BH4987 48J 68JB 1100B
BH5087 49JB 610B
BH51 B7 52J 120JB 620B
BH5287 370B 120JB 650B
BH5387 WB 44JB 1300B
'.," BH5487 250JB 90JB 1200B
BH5587 94JB 1200B
BH5687 SOJB 1100B
East Trenches Sandstone:
BH3987 250J
BH4287 39J 520
BH4487 WB 920B
BH4587 220J
BH5187 B6JB 720B
BH5687 42JB 47JB 1000B
East Trenches Claystone:
BH3987 37JB 250J
BH4OB7 200J
BH41 B7 190J
BH4387 34JB 730B
BH4587 190J
BH4687 350
BH47B7 59JB 1100B
BH4887 42JB 560B
BH4987 580B
BH5087 55JB 690B
BH52B7 280JB 84JB 680B
BHS387 58JB 6706
BHS487 34J6 6506
BH5587 SOJ6 10006
6H57B7 140J 10006
-------
TABLE A.12
TOTAL METALS ABOVE BACKGROUND IN SOlLS1
..
Number of Range of
RIIUts Background Maximum
ADeNe Number of Concentration' Conc8ntnItion- ..
AnIIytI B8ckgrcund2 RIIUIts (mg/kg) (mg/kg)
Aluminum 2 204 10300-25312 70600
AntImony 1 204 ND-16.2 .024-
-Arlenic 35 204 3.6-15.86 37
Barium 6 204 155.8-345.8 1899
Beryllium 0 204 2.2-17.75 1.7
Cldmium 58 204 ND-3.2 6.2
Calcium 31 204 5990-43079 25400
Cesium 0 24 ND-274 NO
Chromium 3 204 10.7-37.9 58
Cobalt 1 204 15.9-29.7 33.1
0' Copper 1 204 19.6-30.62 25
~
Iron 7 204 12300-41295 42700
I.88d 2 204 13.4-34.5 45.6
Uthium 0 20 7.0-44.4 12.71
Magnesium 2 204 2520-6151 5260
Manganese 14 204 305-659 3540
Mercury 1 204 0.27~.58 114
Molybdenum 0 15 11.2-38~65 NO
Nickel 4 204 14.3-56.95 36.1
Potassium 3 204 NO-3336 4170
Selenium 1 204 NO-NO 1.5
Siver 0 211 12.7-40.9 NO
Sodium 2 211 N0-3680 1400
Strontium 0 211 69.2-226 184
Thlllium 0 211 ND-NO NO
TIn - 0 12 268-338 NO
Vanadium 10 211 22.2-58.2 108
Zinc 2 211 52.69-106.7 58
NO
I
2
,
Not detected
ConcentratIOn data obtained from the 1987. 1988. and 1989 field investigations.
Compared to background value for appropriate lithologies. listed in Table A4.
Range of maximum values for different geologic materials.
Reponed when maximum concentration is above background.
-
-------
TABLE A-13
TOTAL AADIONUCUDES ABOVE BACKGROUND IN SOlLS1
.
Number of Range of
Rautts Background Maximum
ADave Number of Conc8ntrationJ Concentratlon4
... Analyt.. Background2 Results (pCI/gm) (pCI/gm)
GrosaAipha 12 227 37-52.302 480
Gross Beta 5 227 29-36.886 37
Uranium 233.234 7 225 0.8-1.985 3.4
'Uranium 235 0 0 0.087.Q.258
Uranium 238 13 227 1.Q.1.675 3.9
Strontium 89.90 10 227 0.4-0.786 1.1
Plutonium 239.240 112 227 0.01.Q.02O 94
Americium 241 118 'lZ1 NR.Q.018 22
Cesium 137 42 227 0.Q.O.113 3.1
.- Tritium (pCl/ml) 11 227 0.299-0,410 0.69
-'
Radium 226 0 9 0.9-1.3
Radium 228 0 9 . 1.1-2.5
NR Not reported
Concentration data obtained from the 1987. 1988. and 1989 field investigations.
2
3
Compared to background value for appropriate lithologies. listed in Table A-3.
Rang. of maximum values for different geologic materials.
.
Reported when maximum concentration i.s above background.
-------
58dl_..t
Sht 10"
N..e..r
50011
50012
soon
SOO2S
5002.
50027
5001.
50021
50010
500)1
s.ct..."t
Sht 1o..
~
50011
50012
500U
soon
5002.
50027
5002.
50029
50010
500Jl
,.u: A-I'
~.~ OH
-..IUU: OMMIIC ~ D£J(UID I. somID"s'
VI..,.I CMoro- Met",.,o..o
CMorldo U"...o C"'orldo Ac.'.".
.wlUl.. .wlUl.. ',,8/a.» 1ulbl
151 I"
ft
47.
UI
U'
221 IJI
III 8J1
III I.
IUI 2201
.. 8J1
Chloro-
_t...".
WLW
60
I9J
I.I.I-Irl-
Chloro-
U"....
'"da.»
Carbon
Jotn-
C"lortd.
..19.t!sl
Irt-
C"'oro-
U"o"o
i!!illsL
oJ
5J
JJ
7J
8
1,1,2-
hlc"'oro-
U"."o
luda~»
'otn-
e"'.ro-
It"...o
iYL!Jl
Cor"'"
OI...I"do
f,,.,..»
6J
1,1,2,2-
'.tra-
C"loro-
U".".
f".I..»
C"'.ro-
n"...o
1!!ILbl
5J
'01.....0
1!!ILbl
IJ
2J
IJ
1,1-0'-
~"'oro-
n"...o
Ju.LUl
(t"'"
..".....
Ju.LUl
IJ
1,1-0'-
CII'.r.-
I tI,o..o
.wL!Il
St,.r....
f...,..,
'0'.'
1,2-0'
C"'oro-
'ono
f..I..,
18
,...,
.,'0..0.
.billIl
7J
1,1-0' -
C"'or.-
n"....
1!!ILbl
1,1-0'-
C"'oro-
're,.".
1!!I.t!JL
2-"'.-
..1..)
12
J9
.
Co.pound .110 detected tn ...oct.ted blan.J - V.tu. ..I.~.t.d below de.ect'oft
Co..co..trotlon d.to obt.lnod fr.. tho '986. 1987. 1988 ond 1989 fl.ld Inv..tl,otlo...
'9\.w-lrop\toblo.\tbt.o.14.
.
-------
TABLE A-15
TOTAL METALS ABOVE BACKGROUND SEDIMENTS!
..
.
Analyte
Number of
ResultS
Above
Background2
Number of
Res&its
Background
~jtJcdion
(mgjkg)
MaxImum
Concentratlon3
(mgjkg)
Aluminum 1 25 24789 24800
AnIImony 3 2S ND . 24.5
Ar8enic 0 24 13.0 4.6
BarIum .. 25 182 300
Berytllum 20 2S NO 15.5
Cadmium 6 25 NO 2.3
Calcium 6 25 72551 132000
CesIum 0 25 NO NO
Chromium 0 25 43.38 26.8
Cobalt 1 25 NO 12
~, Copper 5 25 22.0 40.4
Iron 2 25 28308 28900
Lad 3 25 39.502 66.4
LIthIum 11 24 NO 27.8
Magnesium 4 25 4110 5970
Manganese 4 25 372.20 1390
Mercury 1 20 ND 0.72
Molybdenum 6 25 NO 10.3
Nickel 1 25 29.9 34
Potassium 8 25 NO 5180
Selenium 1 25 ND 21.3
Siver 9 25 6.8 48.9
Sodium 5 25 NO 670
Strontium 1 25 175 179
Thallium 1 25 NO 8.5
Tin 9 25 NO 1080
Vanadium 2 25 50.2 58.4
Zinc 10 25 92.688 735
NO
2
Not detected
Concentration data obtained from the 1986. 1987. 1988. and 1989 field investigations.
Compared to background values listed in Table A-3.
Reported when maximum concentration is above background.
3
-------
TABLE A-18
TOTAL RADIONUCUDES ABOVE BACKGROUND IN SEDIMENTS1
.
Number of
R8its Background Maximum
Atx:Ne Number of Concenb'IItiOn3 ConcenUatiOn3 !
AnIIyte BackgroundZ ReUts (pCI/gm) (pCI/gm)
Gross Alpha 3 12 60 77
Gross Beta 0 12 50 .46
Uranium 233.234 1 12 1.669 2.1
Uranium 235 1 12 0.176 0.2
Uranium 238 1 12 1.735 2.7
Strontium 89.90 0 12 1.390 0.5
Plutonium 239.240 8 12 0.096 0.85
Americium 241 0 3 0.029 0.02
Celium 137 1 11 1.578 0.3
.'
~, TrttIum (pC1/mI) 0 12 0.408 0.18
Radium 226 1 4 1.0 . 1.3
Radium 228 0 4 2.1 1.4
Z
Concentration data obtained from the 1986. 1987. 1988. and 1989 field investigations.
Compared to background values listed in Table A-3.
3
Reported ~ maximum concentration is above background.
-------
-------
'J:
-------
-------
..
.
. ,
APPENDIX 8-1
SURFACE WATER SAMPUNG RESULTS
VOLATILE ORGANIC COMPOUNDS
S.JOtCA:::e WA"'E" ,..~Otl'" OtE"'E:;):A~ ":::""0" P.,A..
~X~ =J.-S ~J.""- 3::"":'=" :~-:):....:..X
e~&~ ..,...''': wa'''''...- a:>~"'c.:>9'
-------
o ~~~ ...
8urface .ater
Volatile organic 8a.plinCj .esults
'03-PAD AND LIP 8ITB
I.I-DI- I.I-DI-
St.,ton 0.'. Chto,.o Ir- V It., , ,,,'.r. ...,.,1.... CerM" ..1.... ..1-
H-'. 58..'.d ...h.... _".n. ,,,,.,'d. .,..... 01...1.. Ac.'.... ....lfl.. .,..... .,.....
I
"'/' .../1 "", .../1 ...'1 .../1 .../1 ...'1 ..,.
0.'- .-..--- .--..-- _0_'-- ...--_.-
sv-oso / / OIlY
sv-oso 0'/21/" till ... HA ... till till till 140 ..
SV-OSO "/11/" 10 U 10 U '0 U 18 " I'" .... IU 'U I"
IV-OSO "/1'/" I..."" Ie I..., ,_I. .. V.,.",. Or..nle A...I,.,. ..., r.~.'''.
511-050 04'''''' 011'
IV-050 OS, 10'" 011'
511.050 01'''/8' 10 U V 10 U V 10 U V 10 U " I U " 10 U " I U " IU " IU "
511.050 01/11/" 10 U V 18 U " 10 U , 18 U , I U " ..... IU , IU , I U ,
511-050 0'/11'" 011'
511-050 0"12'" 011'
511-050 10/0'1" 011'
511-050 II/OJ/" 011'
511-050 12'01'" 011'
511-050 OIlOS/1O 011'
IV-050 0"0"10 011'
511-050 OJ/""O 011'
511-0SI 01'''/'' till ... "" till till till .. 101 ..
IV-051 01/11/.. 011'
IV-O" 0'/"/" 011'
IV-OSI OS,IO/" OIlY
511-051 01'''''' 10 U V 10 U V 10 U " 10 U , I U " 10 U " IU " IU " IU "
511-0SI 0""'" OIlY
511-0SI 08'"'" OIlY
IV-OSI 0"12'" OIlY
511-0SI 10/04'" 011'
511.0SI II ,OJ," OIlY
511.0!U 12/01'" 011'
511-051 OI,OS,1O OIlY
511-051 0'/02'10 DAY
'".052 01'21'" Nil NIl Nil .. till Nil .. 7J till
511-052 OI/U," 10 U 10 U 10 U 10 U I . ,... 'U IU I U
511-052 04/"'" DA'
511 052 05/10'" OIlY
511.052 011'0'/" 011'
VALUE QUALifiERS: NA - An."t. not r.~ort.' U . An."..d ...., ..., ..,..,..
.I . ~r...n' '.Iow ""c"o.. 'I." . . ~r."'" I.. ,.....,.., 11...e
4".II'I.r Ind'c.". d.,. .... "0' ...... ...'1','''.8
- . ",..1... II.. ..., .., I . h"..,.. ...,-
M . '.'e" .,Ie. ..., I.. 1O-11e& r....
. . .'I.e,.8: A. Aec.~"'" .1" ",,""c.'I."'1 ". ".'18
DAtA pAOOR (j(J~litY"'.' I...
ORIGINAL
-------
), ...
,.,
.
..
8urfaae .ater
volatile organio 8a.pling Results
,03-PAD AIfD LIP 81TS
'0..'.1.2. 1.2.0'. a.a.I-Ir' (.rt.." 'r- a.I-D'-
Statloft O.t. DI.loloro .Io'oro c".r. ".r. v.." "c.'.r. ....-
"_er Sa..I... ..".... (Io'.r.'." .ttl.". 1-'...- ....... .101.r''. ....... -...... ........
.,/1 ../1 .'/' ..,. .,'1 .,'1 ...,. ..,. ...,.
-----.- - --.--..- .--------- ---
SV.050 , / DII'
SV. 050 O'/ll/.' 5 U I' 5 U .. I U 1005 .. .. ..
5".050 "/"/.. NIl . 5 U 10 U . .. . ao U IU ..
5".050 "/"'" I...ufflcl..., 5_1. .r v.,..'I. Or,o"'. "".1,... .., r.~.."",
$".050 0'/"/" DII'
S".050 05/ "/" DII'
$".050 0'/"/" 5 U " . v 5 U " IOU " I U " l J " IOU V IU " IU "
$".050 07/"/" 5 U v . " 5 U " 10 U " . U " 10 " IIU " . U v IV V
$".050 08/"/" 0.'
$".050 09/"/" DII'
$".050 10/"/" 011'
$".050 ,,/OJ/" DII'
$".050 "/DI/" DII'
$".050 01/05/" Da'
$".050 01/02/" DII'
$1/.050 OJ/"/tO DII'
5".051 0'/21/" 5 U 5 U 5 U .. IU 21l .. .. ..
$1/.051 "/U," DII'
$1/.051 "/"/" 011'
$".058 05/ ../.. DII'
SI/.058 01/"/" S U " . J " S U v. 10 U " IU " .. " IOU V IU V I U V
$1/.058 0'/"/" DII'
S".058 01/ "/" 011'
$".051 0'/"/" DII'
$I/.DSI 10/0'/" DII'
SI/.OSI II/OJ/" 011'
$1/.058 "/01/" 011'
$1/.051 01/05/" 011'
$I/.DSI DI/OI/tO 011'
5" 052 0'/2'/" 5 u 5 u 5 U .. 5 U 5 U .. .. ..
$I/.OU OI/U/.. H. 2 J S u 10 U a J J J I'. IU I.
$I/.Dn "/81/" 011'
$1/ on 05110/.. 011'
$".on "/09/8' DII'
"ALU( OUAll'IE.$. .. - A".I,.. ".. r.por'.. U - A"..,..d ..., .0' .....,..
J - .r.....' ~.Io. ..t8cttO" ,..tt . . 'r....t 1ft '...r...r, .,...
DA'A VAL'OA'ION OUA"'ERS: Coo ..".."0" q.."".r '"dl..'., d... h.. "01 ..... ..1'..'...)
. . 1101.... 11- ... -, 1 . 1.11_... ...-
. . ...... 0"'. .., ,. IO-IIOS r..,.
. - ..Ject... A. Acc..-..'. .". .M8"flc8tt..... v. ...,.
POOR QUALITY
-------
~,~ ...
8urfaoe Water
Volatile organio ea.plinCJ aesults
,o3-paD MID LIP 81TB
Cle-i. t- Oillr- I,I,I-Irl Ir.".-I.I- 4....,..,1-
$t..,o" 0... O'."loro IrI.Iolor. Cloloro cll'oro D'c"loro 1-...."
"-or ,...,... p'..'''. ."'... ..,...". .t..... .....". ,r.,.... e._f... - 1-110..-
..,'I ",/, ..,'I ..,/1 "/' "", "/' .,'1 ..,.
. -- - ----- --.. - --- ------- .---.'''-'-- -- -.--
$W-050 , / 011'
111-050 07/21/87 .. 00 HA I U ... NIl .. .. ..
$W-050 ",,,,.. 5 U II 5 U IU IU I U I. 10 U 10 .
511-050 ""7'" I...... fl. '0'" 5_'. or Vol.,'I. Or,.n'. A..ol,.,. ..., ro,....'.".
$W-050 00'17/.' 011'
511-050 05/10/.' 011'
511-050 "/'17/.' I U V . V 5 U V I V V IV A IV V IV V 10 V V 10 V .
511-050 07/11/" I V V . V I U V I V ., I U V IV ., IU V I. U V I. U .
511.050 08/"/" 011'
511-050 0""'" 011'
511-050 10'00/" 011'
511-050 II/OJ/" 011'
511-010 12/01/" 011'
511-050 OllOlltO 011'
111.050 OllOlltO 011'
$W-OSO OJ/"/tO 011'
511-051 07/21'.7 HA 11 NIl IV ... .. .. .. ..
III - 051 011"/" 011'
$W - 051 ../11/.. 0111
$W-051 05/10/" 011'
511-051 OI/'17/.' I V V 5 V 5 U V- IV V IV A I U V IV V 10 V V 10 V .
511-051 07/"/" 011'
$W-051 08/ III.' 011'
511 . 051 Ol/l'll" 011'
511 . 051 10/04/" DA'
511-051 II/OJ/" 011'
511.051 12/01/" 011'
511-051 01/01/'0 OA'
511.051 02/02/tO OA'
5W-OSl 07/2118' HA 5 U HA I V NIl HI .. .. ..
$W - 051 01/"/" 5 V . 5 U I U IU I U IU 10 U 10 U
$11-051 04'11/" OA'
511-0U 05/10/" DA'
511-052 06/0'1" OA'
VAlUE QUAll'IEII5: ... A".I,t. ..0' roporto" U . Ano',.." ..., "., "o'.c'o"
J - 'r.....' -.'0. d.,.c'lo.. "." . - 'r...~t ,,, ....r...r, .....
DAIA VA' 10.1 ION QUAI' lIAS: 1"0 V8"..'ton .u...f'.r end'c.'.. de'. ~e' ftot.~.." .."..,...)
. . 110''''''1 ".. "0' ..t I . I."."" ".,-
M . lot... 0,'8. .... ... 1O-11Oa ro.,.
. - ..J.c,.., A. Acc._'..'. .... 4u.'tftc..to"I' V - V.t..
OOR QUALITY
r\MII"It.1 A.I
.
-------
~.~ .-
surfaae Water
Volatile organio s.-pling Results
'O]-PAD AltD LIP SITB
1.tr8 1.1.'.'-
St.,ton 0.'. ch'oro ,.....111... CIII... ....,. ,...,
"....r So..lod .'h.n. .,,,.... 10'Uln. ........ ....... 5'",,,, .,.....
.,'1 .,/1 ..,,, .,1' ..,,, .,,, ..,I'
..--- .-.---- .._--- -- ------ --
5\1-050 , I l1li,
5\1.050 01'''''' 6S HII Nil l1li l1li HII l1li
5\1.050 0""'" 50 I V 5 U IV IV I V IU
5\1.050 ","/.. Inautttet...' S...'. or V.I.ttl. Or,.nte ""01,... ... ".."."H.
SW.050 01/11'" l1li,
5W-050 05'10'" l1li,
5W.05n 0""'" II Y I U Y 5 II " I U " I U " I U " IU "
5\1.050 01111/" It Y I U Y 5 U Y IU " IU " I U " IU ,
5W.050 08/11/" 011'
5W-050 0',U/8' l1li,
5W-050 10'01'" DII'
5W-050 11'01/" DII'
5W.050 U/OI/" l1li,
5\1-050 01/05"0 l1li,
5W-050 0"0"10 DII'
5W-050 OJ/I1"O 011'
5W-OSt 011,.'81 .. NIl Nil .. .. .. ..
5\1-051 0'1"'" 011'
5W-05' 01/11'8' l1li,
5\1-051 01'10'" l1li,
5\1-051 01'''''' ' Y 5 U Y 5 U " SU " I U " IU " IU "
SW-051 01'18/" 011'
SW-051 08/11'" l1li,
SW-051 0" U,.. l1li,
IW-051 10'01'" l1li,
5W.051 II,OJ'8' l1li,
5W-051 "'01'" l1li,
5W-OSI 01'05"0 011'
5W - OSI 0"02'10 011'
SW.OS, 011'1/81 5 II HII Nil ... Nil Nil ..
SW-OIZ o.,u,.. 2. 5 U 5 U I V IV 5V IV
swoon 01'"'" 011'
5W-OSZ 05'10'" l1li,
5W-OSZ 01'0"" l1li,
Y"IUI QU"II'111I5: Nil. "nolrl. "01 .opo.lod U. ""olr,od .... ".. d...c...
J . 'r.....' ...10. 4.'.ct 10" I'." . . 'r.....' 'ft ,.~.,....,., .,...
OAIA VAIIOAIION QUAI'IIA5: (Ho .011'0110" q.ollflo. Indl.olo. do" ~o. "0' ...." "o'ldo,,".
. . 1101.1.. ..- "01 -. . . ....-... .......
M. ....11 .,1.. ".. I" IO-IIGS r..,-
II . lIoJo.I'" ". ".eoplo..l. .1.11 ..""'.0.10..,
POOR QUALITY
ORIGINAL
.
" . Volt.
-------
'G3-PAD AND LIP SITE
Stet Ion 0.'.
NU8ber 50"'0"
SW-Ou 01/01/"
SW.O" 08/11/8.
SW-O" 01/"/8'
swoon 10/0./.'
511.052 11/01/.'
511-052 U/OI/..
511.0SZ 01'05"0
SII.on Oz/o".o
sw-OSZ 01/" /'0
511.055 0'/'1/.'
SW.OSI O'/ZI,.'
511.051 01/21/.1
511.051 0'/"/.'
511.051 OS/25'.'
511.051 01"1/.'
511-0SS 01/18/..
SW.OSS 08'1""
511-051 0'/'0/.'
511.0SS 10/1./1.
511.051 II /0./..
511-0SS U/01/..
511.051 01/11/'0
511 051 o,/n/.o
511-051 01/15/'0
511-05' O'/ZI/.'
III.OS1 OI/n/..
SW.OSJ 01/.,/.,
SW.OSJ 01'10'.'
511 051 01/0'/.'
111.051 01/0""
III - 051 01/11'.'
511 -051 0"11/"
511-05' 10/01'.'
III.OSJ II /01/..
(h'orO
"'''.''8
Ir-
-,......
.1/'
u,/'
...------
.. ------..--
011'
011'
011'
011'
011'
011'
011'
011'
011'
HA
HA
volatile
"...,.1
(..,.,1".
../1
HA
J. ...
..,
8urface .ater
organic 8a.pling
("'.r.
.,.....
../1
l1li
.esults
...,.."....
c'-.,,,.
../1
C.r""
010."".
.."
1.1-01-
c..'.r.
........
.."
1.1-01-
c"lor.
.,......
..'I
Acet.".
..1'
---
.._---
--
l1li HA .. 110 ..
1 . 5 J' I U 1 U I U
I U " I J " I U A IU A IU A
1 U " 10 U V 1 U V S U V I U V
S U " I JI I IU V IU , IU ,
I JI A . J8 A I U , I U , IU ,
s U 10 U IU IU IU
s U 10 U IU IU I It
s U 10 U I U IU IU
".av',le'8n' 50""'. or "0'0"'. Or,o"'c "".1,. to ..., r......'.".
10 U 10 U Z J 10 U
10 U " 10 U " 10 U " 10 U "
0.'. 1101 yet r.c.I"8d
10 U II 10 U " 10 U II 10 U II
10 U II 10 U " 10 U II 10 U ,
10 U " 10 U II 10 U V 10 U ,
10 U 10 U 10 U 10 U
10 U 10 U 10 U 10 U
10 U 10 U 10 U 10 U
O.t. not ,.t recel"8d
D.'. "0' ,., recel".'
Do'. "0' ,., r.ce' w.ct
0.,. not ,., recetveet
"A
OIlY
DA'
DAY
DAY
DAY
DAY
DAY
DAY
DAY
HA
HI
MIl
"AlUi QU"ll'IIA5, HA. "...1,.,. "., r.,or'." U - A..ol,.... 'U' ..., ".'.c''''
J . Pr..."' ..10. ".,.c'lo" It.I' I . Pr.....' t. I...r.'.r, .,...
0"1" ""lIDAIIOH QU"I'IIAI, (Ho v.lt...,to" quolt.t.r t"'lco'.. d... "00 ..0' ..... V",,,.,.,,.)
POOR QUALITY
ORIGINAL
MIl
HI
.
48
MIl
- . ...,..,., tt- ..., -, 1 . I.tt-,,,, ...,...
" - I.'c" ..,.. ..., t.. IO-I~ r....
8 - I.J.c'."1 ". Acc..'.". ..,. ....'t"c.'I."OI ". "..,..
.
-------
'G3-PAD AIID
St.tlon Olio
"_or So-,Iod
SV-OU 01/01/"
SV-OU 08/11/..
SV-051 0'/"/"
SV-051 10/01/"
SV-OU II lOJ/..
SV-051 12/01/"
slI-on 01/0"80
SV-051 0"0"80
SII-051 OJ/I1/80
511.055 01121/.'
IV-on 0'1'1/.'
sv - on "'''/''
sv.on 01/111"
sv-o's oS/n/"
sv - OSS 01/28/.'
sv.OSS 01/11/"
SII-05S 081 III"
SII-O'S 0'/20/.'
sv-OSS 10/1""
SII.05S 11/0""
SII.O'S 1"01'.'
SII.OSS 01/11/'0
511 oss o"n/o
511.0SS OJ/I'/.o
511.051 01/'1/.'
511.051 oi/U/"
511.0" 01/''/"
511-051 OS/IO/.'
511.051 01/0'1"
511.051 01/011"
511.051 0./11 I"
511-051 0" ",.,
511-051 10/04/..
511-051 II lOJ/.'
LIP 81TS
,.ul-I,'-
Olellioro
o'''.n.
u,/I
Ch'oro'.",
.,'1
Volatile
1.2-01-
.1110..
.'h.".
u,'l
.~...
sur.faca ..tar
organic Sa.pliDg
Results
- . -.. .'n on
011'
011'
011'
011'
011'
011'
011'
011'
011'
,
,
I. I. I-b' Corlton 1.- I,I-De.
....... 10'.. ve.,1 "cIII.r. ....-
1-"'''- ........ c"'.",. ac...e. ....... ........
...'1 .". uti' "", .", ...,.
.-- .-----
, u I U 5 U .. I U S U .. .. ..
h,.ut'lcl.,,' S...,. or V.I."'. Or,.nte "".'''.'' ..., ._n''''.
III , U , U 10 U I U 'V 10 V I U IV
, V " 5 U " , V " 10 V . I U " I V " 18 U " 'U " ... "
De'8 "ot r.' received
5 U V , U V 5 V V 10 V V I U V 5V V 10 U V IV V I V V
I U V S U V 5 V V 10 U V . U V . U V 18 U . 'U V ... .
I U V S U , I U , 10 U , I V V I U V 18 U . IU V I" V
I U I U 5 U 10 U I U I U 10 U IU ...
II , U 5 U 10 U I U S U 10 V IU 'V
, U , U , U 10 U . U I U 10 V 'U . U
De,. not rot roc.t"...
Do.. ..., ,., ..c.I...'
0... ..., ,at roc.h,..
De'e ..ot ,at rocet"."
, U 5 U , U .. 5 U 5 V .. .. ..
011'
011'
011'
011'
011'
011'
OA'
OA'
011'
VALUE QU~ll'I(AS: HA. An8"'. "0\ roported U - An.trled but no' ..'oct"
~ . Pr...,,' ~.'o. ..'actfon ..... . . 'r.....' .. '."ro'or, .,...
OAIA V"IIO"'ION QU""lfA5: 1"0 ...Id.olo.. qUII.'... ...dle.'., d.'. h.. ..0' b... ...1".'.'..
. . HoI.... ,... ..0' .., a . a.,...,.. ...1..
" . I.'e. .,111. ..., I.. 80-1'" ,..,.
. - '.J.el.', ". "ce.,...'. w"" .u.""C.".""'
POOR QUALITY
ORIGINAL
-------
'G)-PAD AND
51.'10" D...
H_er 5...10"
._-- -------
$W-on 07/07/8'
$W.on 08/11/"
$W-on 0'/"/"
$W-on 10/01/"
5W-On 11/01/8'
$W.052 11/01/8.
$W.on 01/05/'0
5w-On 02/02/.0
5W-On OJ/I7/'O
511.055 0'/21/8'
$W-OSS 0'/ZI/8'
$W.OSS 06/21/88
$W-OU 01/17/8'
$W.OU OS/25/"
5w-055 "/"/"
$W.OU 07/18/"
5w-OU 08/1'/"
$W-OU 0'/20/"
$W-OSS 10/11/8.
$W-OSS II /0./..
5W-OU 12/07/"
511-055 01/11/.0
5W.OU 02/21/.0
5W-OS5 01/15/tO
511.057 0'/21/8'
511-057 "/21/88
$W.057 01/17/8'
511-057 05/10/8.
511-057 06/0./8.
511.057 07/07/..
$W-057 08/11/8.
$W.057 0./16/8.
$W.OS' 10/01/"
511.057 11/01/"
LIP SITB
[I.-I."
Oleh loro
p'.".".
.../1
Idellioro
........
...'1
.-----
01'
01'
01'
01'
01'
01'
DII'
01'
01'
Volatile
OU,r-
e,,'.re
..'h...
.../1
___0.-
. 4;-~ .-
surfaae Water
organic sa.pling
1.1.I.Ir'
c.loro
.n....
...'1
I......
.."
Results
Ir....-..J-
Olc.'or.
,r.,...
...'1
Ir_t...
.."
.....,.,.-
1-...'.
....
../1
1-"'.."-
.."
HA 5 U HA I U ... HA ... ... ""
I"."f"ct.nt S...,. or '010.110 O.....le ."01,... .., ro"....'...
5 U 17 5 U I U I U 5 U I U 10 U 10 U
5 U " Ie " 5 U . I U . I U " IV A Iv A 10 U A I' V A
DolO ..0. '0' recel....
5 U , 19 V 5 U , I U V IV " 5 V V I V V 10 V V 10 U .
I V V II V I U V IV V IV V IV V IV V IIV V I'. .
5 U " 2. V 5 U V I U V IV A I V V IV V I' V V 10. V
5 U 2. 5 U I U I V I U IV I. V I. V
5 U 5 U 5 V . U 5 V I V I U IIV II.
5 U 65 5 U I U IV IV I V 10 V I. V
0... "0' ,.t rlcetv..
0"8 ..., ,., roe.ho.
Oa.. ..01 ..t rlc' ,,,..
0.10 ..0' ..t rlC' t wed
NA
01'
DII'
OA'
OA'
OA'
OA'
01'
01'
01'
s U
HA
I U
""
HA
..
VALUE QUALlfl(AS: HA. An8_," not report.d U . An.t"ed 'ut ...t 4."c'"
~ - 'r.....' ~.'ow ~,"c"on ".It . . 'r.....' tR ',"r.t.r, ....,
OAIA VA' IOAIION QUA.'lfA5, (Ho vol"'llo" qu.II'lor I..dl..,.. d.l. h.. "0'.."" v.II".,...)
. . "".'" tI- "0' -, 1 . l.tI_... v.""
" . '..e. .,1'. .... I.. eo.11Ga r....
A . ..Joe'..1 A. Ae.."..lo .1'. "".'ltle.'I''''1 V. V.".
POOR QUALITY
ORIGINAL
~
..
...
-------
9G)-PAD AND
Stet ton 0.'.
"_.r 5.....d
.--...---
SW-on 07/07/8.
sw-on 08/11/"
511.052 0'/18/"
511-on 10/04/"
111-051 II/OJ/..
111-051 Il/OI/"
111.051 01/01/'0
111-051 01/01110
III.on OJ/" /.0
SII-OSI 01/'11/"
111-055 07/21/11
SW-OI5 01/"/'1
111-055 04/11/..
111-055 05/15/1.
511-055 H/ZI/..
111-055 07/11/..
511-055 08' If/..
III - 055 0./20/..
III-OIS '0/"'"
111-055 11/0./..
III-OIS 11/01/..
111-055 01/"/10
111-055 Ol/U/tO
111-055 OJ, IS' to
511-051 01/'1'/81
111-051 H/2I/1I
111-051 04/11/11
111.057 05/10/8.
III 051 01/0'/11
511.051 07/0""
111.051 08'11/"
111.051 O'/If/II
111-051 10/04/11
111-051 II,OJ/II
LIP SITE
tetra
c"'oro
.'h.".
J' .-
..,
4
8urfaa. ..ter
Volatile orgaDia 8a8pliD9 a.sults
u,/I
1.1.2,2-
'.treel,'oro
.,...".
.".
101"8"1
.",
U".I
........
",',
51,r....
..."
,...,
..,....
",,,
tlll.r.
,......
u,"
..-.-
._---
-.-.--..---
---
PII'
01'
01'
...,
01'
...,
01'
...,
...,
5 u till HA .. .. Ht ..
......"Icl..., s..... or Vola'.'. Or,ante Au'"" .... r~....t...
2 J 5 u I J I U I U 5 U I U
s U A 5 U A 5 U A I U A IV A I U " IV "
Det. not rot raeetvld
5 U V 5 U V 5 U A I U " I U A I U " IU A
I U " I U " I U , IV , I U , IV , I. ,
5 V , I V " 5 V A IV " I U " . V " IU "
I U 5 V 5 U I U I U . V I U
I U I U 5 U I V I V 5 V IU
I U 5 U I U IV I U I U IU
0.'. not rat racalva.
D.'. "., ,., recelv..
0.,. not rat racalv..
0.,. not rat rlca'vld
5 U
01'
01'
OA'
DA'
OA'
DAY
DA'
OA'
OA'
HA
HA
Nt
..
...
Nt
"ALOE QUAL If lEAl, HA. A..."I. .... r.port.d U. A".,,'.d bu' ...t ..t.c..'
J . .r...ftt ~.'ow ..'.C"OR ".1' . . 'r...,,' In '."r.'.r, .,...
OA'A VAL.OA.,ON QuAlf'EAI: (Ho ..".."0.. qu."".r ,..dle.t.. d... h.. "01 b.... ..,.......)
. . "',...., t'" ..ot ..I I . I.t'",,, ...,".
H . I.tell .,,,. ...t I.. 8O-IZOIL r.....
. . ..J.c...; A. Ace.".",. ..." ~u.""c."o".1 ,. ".1..
POOR QUALITY
()QI~I~'AI
-------
,O]-PAD AND LIP SITE
Stet'on 0.'. (hloro
.......r So.".. ..th....
u,/I
5W-057 12/01/89 011'
5W-057 01/05/'0 011'
5W-057 02/02/'0 011'
5W-057 01/17/'0 011'
5W-058 07/ZI/87 HA
5\1-058 Ol/U/" 10 II
5W-058 04/17/8' 011'
5W-058 05/10/81 011'
5W-058 01/18/" 10 II "
5W-058 07/14/81 OA'
5W-058 08/11/81 011'
5W-058 0'/20/81 OA'
5W-058 10/04/89 OA'
5W-058 11/20/81 OA'
5W-058 12/01/81 OA'
5W-058 01/05/'0 OA'
5W-058 02/02/.0 OAf
5W-0" 06/ll/88
5W-0" 01/10/"
5W-0" 05/11/..
5W. 0" 06/27/81
5W -0" 07/18181
5W-O" 08/11/81
5W.0" 0"20/81
5W-0" 10/04/81
5\1-0" 11/0"81
5W.0" 12/01/81
5W.0" 01/05/tO
5W.0" 02/02/tO
5W-0" Oil II/tO
,.. ...
-',
surfaae water
Volatile organic Sa.pling aesults
1,1-0'- 1.1-0'-
8r- V'n,I C"I.r. ...,..,1.... C.r"'" c"l- c..t....
........ C" '.rldo .,,,.... ("'.rl'. Aceton. Ote.If'.. .,,,... .,.....
u," u,/I u,II u,I' utI' ..,/1 ..,'I .."
-------. ._---- -- ---
HA HA .. l1li l1li .. 'U l1li
10 II 10 II 10 U 1 I 7 J8 .11 IU .U
10 II V 10 II " 10 II II 2 JI ,. II II Z J II I U II 5 II II
10 II 10 II 10 II 10 II 1 I 1 JI I U . 1 J
OIl'
011'
10 II II 10 II II 10 II II - 10 II II 5 II V 12 II J J II I U II I II II
OA'
10 II II 10 II II 10 II II 10 U II I U II 2 J8 II IU II IU II IU II
OA'
011'
OA'
OA'
DA'
OA'
0." not re. received
~~IU( QUAl If If AS: HA - Ana'". not reported U. .n."..eI but n.' ....c."
J . 'r...n' b.low ..'.ctlon ...tt . . 're....t IR '...r.t.r, .....
OA'" VAliDAtiON QUAlfIlA\: (Ho ..,.Ild.,.O" qu."fter 'ncllc.'.. de'. h.. "ot b.." v."tI.,...)
. - ...'.1.1 ".. ..., .., I - I.t,..t.. ...,...
. . I.tc" .."0 n.' ,.. 8O-1~ r...,.
A - AoJoet..: A. Aceop'..I. .".. ....I"'C.".".I II. v.I..
POOR QUALITY
ORIGINAL
.
-------
903-PAD AND LIP 8ITS
'0181-1.1-
Otc,-Ioro
St.,'on
0.'.
"""0"
.'''.n8
Chl.r.'.'"
..."
MU8ber
..,/1
. J' ...
-,
Surfaae .atar
Volatile orgaaia Sa.pling a..ult.
1.2-01-
c"ar.
...,.".
'-""0.-
..,/,
I.I.I-'rl
c.'.r.
.,......
","
Carlt...
her.
c"'orl".
...1'
VI."
ac"",
","
,.-
.Ic.'.r.
_1I.c..
..,,,
.
I.I-DI-
c."'"
........
..I'
$W-O~7 "/01/" 011'
5'1.051 01/05/10 011'
5V.057 01/01/10 011'
5V-O~7 OJ/" /'0 011'
SII.O~. 07/2'/.7 5 U I U 5 U .. I V I V .. .. ..
5'1.051 o./n/.. NIl , I V 10 U I V , 10 V IV ..
SV.OS8 0./"/8' OIlY
SV.OS8 o~/ 10/., OIlY
SV.058 0./,./8. 5 U V 2 J A 5 U V 10 U . I U V I J II 10 U V I V V I U V
SII.058 07/1./., OIlY
SII.OS8 08/ ../., 011'
SV.OS8 08/10/.. OIlY
5V.OS8 10/0./.. OIlY
SW-058 "/201" OIlY
SW. 051 "/01/" 011'
SII-058 01/05/80 011'
sv-OS' 01/01/80 011'
SII. 011 0./22/8. "A 68 5 U 10 U . IV 10 U IV I V
5'1.017 0'/10/" OIly
5'1- 017 05/ ../.. 011'
5v.077 0'/"/" . V J J A ~ U V 10 U . ~ V V ~ V V 10 V V I U V I U V
SV.017 07/../.. OAY
SV. 017 08/ ../.. 5 U V 5 U V ~ U V 10 U V I U V 5 U V 10 V V I U V 5 U V
SII.017 08/20/" DA'
SII.017 10/0./.. 011'
511 017 .. /0'/" 01'
511.017 12/01/" 011'
SV.017 01/05/'0 DA'
SII 017 01/02/90 OA,
SII 011 0./ ../10 0.'. not ~.t rec.lved
.../1
....- -----._u-
YAlU( QUAllfIIAS: HI - An.'". not report.. U - AnalY'8d but fta' ..'.ct..
J. 'r...n' ".'0. ~.t.ct'O" It-It' - Pr.....' ,.. '."r...rr .,...
DAIA VAIIOAIIOH QUAI' liAS: 1"0 vcl'''o.'o" quoll'l.r Ind'co'o, do'o h.. "0' bo.. v.'I..'....)
POOR QU.AUTY
()RI~INAI.
---
...__0--
. - Me'.'Rt ,t.. _0' .., I - I."",.. ..,~.
N . I.tch apt'. n.' tft 8Q.I20S r....
. - '.J.C'..I A - Acc.,I..lo wll. .uc'lflc.'I...,
-------
'03-PAD UD
St."O" 0.,.
"_er 5...,lod
511-057 12/01/"
N-057 01/05/tO
511-057 02/02/tO
511-057 01/17/'0
SII-051 01/21/"
N - 051 "/U/"
511-051 04/17/11
511.051 05/10'/11
511.05' 01/2118'
511-058 07/"/11
511-058 08/11/11
511.058 0'/20/11
511.058 10/0c/1I
511.058 11/20/11
511.058 12 101/11
511.058 01105/'0
511-051 02/02/'0
511.0" 06/22/18
511.017 01/10181
511.017 05/11/"
511.017 01/27/11
511.017 07/18/81
511.017 01/11111
511.077 0'/20/"
511.077 10/04/11
511.077 11/0'/11
511.017 12/01/11
511.017 01/05/'0
SII 017 02/02/'0
511.017 01/11/'0
LIP SITE
C:h-I.I-
Olc"lo.o
"0'.'"
11,/1
. . - -----
OIl.
OIl.
OIl.
OIl'
HA
5 U
OIl.
OIl.
5 U Y
OIlY
OIlY
OIl.
OIl.
OIl.
OIl'
OIlY
OIl.
5 U
OIl.
OIl.
5 U V
OIlY
5 U V
011'
OIl.
OIl'
OIl.
011'
DA.
s. .y
'"
....- . ... -
SUJ:'faoe .ater
Volatile organio sa.pling ..sults
0''''0810 1.1.2-'.' "....-1.1- C-Me''',,-
Ir'c..'oro c"'oro '''Ior. O'c"lo.. I-pe."
.,..... ..,...... .,...... .....". ,...,... Ir_'," .... 1-"'..--
",/, ""I ",/1 ..,. ",/1 ..II .,'1 ..'I
.----- ------
I U "" IU .. .. .. .. ..
I I U IU IU I U I U 10 U 10 "
5 U V 5 U V I U V 5 U II 5 U V 5 U V 10 U . 10 U .
2500 5 U I U I U 5 U IU 10 U 10 U
47 II 5 U V IU V 5 U II 5 U V IU " 10 U . 10 U .
I U Y 5 U V IU V 5 U II I U V IU " 10 U V 10 U V
0.,. not yet r.c.'ved
YIIIU( QUIIII'I[AS: HA. lI.olyto .ot roporto' U . IIn.',.od "lit .., ..,.C,..
J . '.0.0.' ...10. 'o'oc'lo. ".1' I . ""0.' ,. ,....r.,.r, .,..,
OA'A YAIIOAIION QUAI'IIAS: 1"0 ..'14"'0. ~".'I"o. ,..dleoto. d... ".. ..~, boo.. "0"'0"'.)
. . Me,,,., ,,- ..0' -, 1 . 10"-'" "0'''0
. . I.,c" .,.t. ..., ,. 10-1'" ro...
. . 'oJoclo" II. IIceo,""" .1'" ...ol"Ic."o"" V. V.".
POOR QUALITY
()QI~I~Ii\1
.
-------
.. .M
'"
surface .a~er
Vola~il. organic s..pling R.8UI~.
'G)-PAD AHD LIP SITB
'etra "'.2.2-
St.tlon O.te e"'oro '.'rae"lero CIo'.... "10" ..,.,
H_.r S..,I.. .th.". '.,,,... I.lue". ....... ....... 5t,r.... ."....
..,'I ",'1 "'/' ..tI' ..." ...,. ...1'
~ - ....---...- .----.-- -- ---
511-05' 12'0"89 on
$V-o" 0"05'" 011'
$V-o" 02'02'" l1li,
$V.os, 0""'" l1li,
$\1-058 0"21'8' 5 U l1li HA l1li l1li l1li NIl
511.05. 01/21/" II 5 U 5 U . U I U 5 U IV
511-05' 0""'" l1li1
511-051 05'10'" 011'
511-05' 01'2"" 5 U , 5 U V 5 U " . U " 5 U " 5 U " I V "
511-05' 0""'" 0111
511-058 01/11'" 011'
511.058 0"20'" 011'
511.058 10'01'" 0111
511-058 11'20'" l1li,
511.058 82'0"" 011'
$V.05. 0"05'" OAI
$V. 058 02'02'" 011'
$11.0" 06'22'88 .. 5 U 5 U IU . U 5 V I V
$V.O" 0"'0'" OA'
$V-O" OS, "'1' 011'
511.0" 01'21'" 5 U , 5 U V 5 U " I U " I U A 5 V A I V "
511-0" 0"'8'" l1li1
511-0" 01""" 5 U Y 5 U V 5 U " 5U " 5 U A 5 U " IU "
511.0" 0'/20'" OAI
511-0" '0'01'" 011'
511-0" II '0"" l1li.
511.0" 82'0"" DIll
$11-0" 01'05'10 OA'
511.0" 02'02'" DAY
$11 0" 0" "'90 O.t. not r.t rec.lved
'AlUI QUAllf11A5: HA - A...lrt. ..ot r.porl.. U - A...lr". ....t .0' ..,.C,..
J - Pr.....' ...loM ..I.c"o.. 1'0'1 . - pr.....t ,. ""r.'.., 10'...
OAtA VA'IOAtION QUAl'IIRS: (Ho _.114atlo" .v."fl.r Indlcet.. date h.. n.t b..R va'lda'..,)
. . ...,.... II. "01 .t . . ..".,.. ...,-
M . ..tclo .p'" ..., ,.. to-'IDS .....
. - A.J.cl'.1 A. Acc.p"Io'. ."10 ~""'c.t'O"'1
POOR QUAUTY
ORIGiNAL
.
v . y.II.
-------
Stet ton 0...
STATION 53
N_er
W-OSJ
W-OSJ
SW-OSJ
Sw-OSJ
sW-OSJ
SW- OSJ
swoon
W.OSJ
sw.on
swoon
sw-OS J
SW.OSJ
SW.OSJ
SW-OSJ
S.,.lod
-----_._~
01/21/"
.,./n/..
.,./n/..
O./OS/89
oS/n/89
06/21/89
01/1"89
08/15/89
0"20/"
10/12/89
11101189
12/1S/8'
01/11190
02/1J/90
. J,' ...
'"
Volatile
Surface Water
organic Sa.pling
C"loro Ir- 'I..yl Cllloro """ylo..o
_tha". _'ho..o Chlorldo o'''ono Ch1orl"
..,/1 .../1 ""I .../1 ..,/1
-----_.- --..--.---- ._--- --.- ---
Nil Nil
10 U 10 U
S_Io or Yolo'"o O.,o..Ic
10 U , 10 U
10 U , 10 U
10 U A 10 U
..
10 U
no' rOlll"o,"'.
10 U ,
10 U ,
10 U A
..
6 I
Nil
10 U
In''''tleto..'
10 U ,
10 U ,
10 U A
OIlY
10 U ,
10 U
10 U
Ooto "0'
Doto "0'
Oa'. "ot
O.'a no'
AII.1r.lo
,
,
A
S I A
. I A
I U A
10 U ,
10 U
10 U
rot rocol"od
yo' rocol"od
,.. receive'
,et receive'
10 U ,
10 U
10 U
10 U ,
10 U
10 U
5 U ,
I U
5 U
aesults
"1-01- 1.1-01-
Cor..on eh10ro .'10r.
"C8'0". Oh.1fl.o 0'''''0 .'ho..
.../1 ..,/1 ../1 .,'1
.. NIl , U ..
. JI I U IU IU
I JI A 2 J A I U V I U ,
10 U V IU V IU V IU ,
II A I U A I U A IU "
J J A 5 U , I U , 5U ,
. JI I U IU IU
10 U I U I U I U
'AlU[ QUAllfl[IIS: Nil. A..ol,to lIot .oportod U . A..ol,.o' ....t no' '.'oe'.'
J . Pro.o..' "010. .otoe'lo.. II.lt I . Prooo..' III lo"oro"rr "Ion'
OAIA 'ALIDA I ION QUAlfl[RS: INo "oll.otloll ....olf'Io. I..dlc.'o. d.,o h.. ..ot boo.. "011'0'0'.)
. . ...1.1., tI- no' -, 1 - lotl-'" ..01..0
" . lotch 0,1'0 ..0' III lO-alGl ro...
. . .0Joe'od: A - Acco,'o"l. .I'h ",..011'leo,Io..ol ,. Volf'
POOR QUALITY
()CI~It\IAI
;
-------
S....on D.'.
STATION 53
Hu...r
5W-OU
N-OU
N-051
5W-051
5W-051
5W-OU
SW-OU
SW-051
SW-051
SW-051
SW-051
SW-051
SW-OU
SW-OU
Sa...lad
..-.-.---
07/21/87
01/21/88
0./21/88
04/05/89
OS/23/89
06/26/89
07/1./89
08/15/89
0./20/88
10/12/88
11/07/8.
12/15/89
01/17/80
02/U/8O
I,.~ ...
.
Volatile
Surface Water
organic sa.pling
aesults
10181-1.2-
Oletlloro
a'tI.n.
u,/I
1.2-01-
c"'oro
a'''en.
u,/'
I-I..'a.....a
.1"
Chloro'o""
"./1
--.._---
---
..-.---.---
, U 5 U 5 U ..
... II U II U 10 U
1..1.."lcla..t Sa..I. or Vola,11o Or,enle A..al,... _t r."....'.".
27 y 5 U V 5 U " 10 U .
5 U V II U " 5 U V 10 U V
27 A II U A 5 U A 10 U .
0111
5 U V 5 U V 5 U V 10 U V
, U II U 5 U 10 U
4Z 5 U 5 U 10 U
0... no' ,et r.c.lved
Dat. ..ot ,a' received
o.ta ..ot "at reeetve"
Oata ..ot ,., rece'ved
VAlU[ QUAll'I(AS: H.. An"rt. RO' r.por..d U - Aft"y..d but ftot ..teete4
J . Pre.eftt "'ow 4e'ecttoft II.It . . 're..nt tR 1.~r.tarr .'8R'
014114 VALIOAIION QUAI'IIA5: (No .all.a'lo" "..a'tflor l..dlcat.1 da.a haa "ot b.a.. .ol'.ata..)
POOR QUALITY
ORIGINAL
I.I.I-Irt C.rboR Ir- 1.1-01-
ch'.ra latra "to.,,1 "ch'oro ah'ar.
.tha... chlorlda Acata'a _tl..... ,ra,...a
"I" "1/' "I" ../. ..,.
I U 5 U .. .. ..
IU II U 10 U I U I U
5 U " 5 U " 10 U " I U V I U V
IU " II U V 10 U V . U V . U V
IU A IU A 10 U A II U " . U "
I U Y 5 U " 10 U " I U Y I U "
I U II U 10 U . U . U
I U 5U 10 U I U IU
. - "'1411'1 t'" not ..t I . I.t._t.. .,alue
M . tatch .,I.a ..at I.. 10-1'" ra....
. . .0J.ct..1 A. Acco,ta.'. .Ith "...'I'Ica.lo..a.
-------
STATION 53
5,.tto"
H_or
SW-051
sw-on
511-051
511 - on
511-051
511-0n
511 - on
511 - on
511-051
511-051
511-05J
511-051
511-051
511-051
0.'.
50"'0'
"- .---------
07/'1/87
01/21/"
01/21'11
04/05'"
05/'1/11
01/21/11
07'"'"
01'15/11
0./20/11
10'12'"
11'07'"
12/15'"
01/17/.0
02/11"0
~.', ..
Sur race .ater
Volatile organic Sa.pling Results
(10-1,1- Olbr- 1,I,2-Irl
Olchloro 'rlchloro cll'oro ehl.ro
,rop.". ~t".... ..,,,.,,. .th.".
10'1/1 ...'1 u.,1 u,'1
..---"-- ----.--
HA
5 V
h..u f" ct ....
5 V v
5 V v
5 V "
011'
5 V v
5 V
5 V
00'0 ..0'
De'. not
0"0 ..0'
De'. not
!I V HA
2 J 5 V
So...l. or volo' It. Or.o..lc
It V 5V
2 J " !I U
!I V " !I U
"..01.01. "0'
II
V
"
I U
. U
r.~u.ot8',
. U II
I U II
I U "
5 U II
I U
. U
V"LU( QU"LI'I(15: HI. "..olr'. "0' r.por'.' U . "..olr.od bu' .... '...e."
J . 'ro....' '.Iow d.'.c.lo.. I'." I . 'rooo..' I" 'o..r...r, "0'"
0.1. V"LIO"IION QU"L'I(A5: eHo voll'o'lo.. quollf'.r I..d'.o'.' '.'0 ho. "0' b.o.. voll'o.".)
5 U V
5 V
I J
r.' roc.lvod
'0' r.oc.1 vod
.0' roc.'voet
rot roc otvoet
5 U V
!I U
!I U
're..a-I.I.. 4-""h..' -
Dlchloro '-".'0
....... pro,.... I..-f... .... .-.....-".
..." u." ...'1 ..." ..II
HI .. .. .. "
!I U 5 U . U 10 U 10 U
5 U " 5 U II 5 U V 10 U V 10 U V
I V " . U V . U V 10 U V 10 U V
. U " . U " . U " 10 U II 10 U II
5 U " 5 V V . U V 10 U V 10 U "
I U . U . U 10 U 10 U
5 U 5 U 5 U 10 U 10 U
. - Mol..., .1.. ..0' .., ( - (0""'" ..0'..0
" . lo'ch op". .... .. IO-IIGS ro...
I . 10Joe'odl ". "ec.,'o'l. w"h ~uol'f'co"O"OI
" . V.It.
-------
STATIOH 53
S.."o"
N-er
SV-05J
SV-05J
SV-05J
SV-O,J
SV-05J
SV-OS)
5".051
'''-0''
5".0"
SV.OS)
5"-OSI
5"-0"
5"-0"
. 5"-0"
0.,.
'o..'.d
.--- ----
07/"/.7
"/U/M
"/U/M
0./05/.'
O'/2J/89
0./26/89
07/"/.'
0./15/.'
0./20/..
10/12/.'
11/07/89
12/"/.'
01/ J7 /.0
02/n/,0
l.tr.
c"'oro
at...ne
--.-
u,/I
s u
s U
I",,,"'e'...'
S U V
S U V
S U "
011'
, U V
S U
, U
0... ..0' ...t
Ooto ..ot ...,
0.'. ..0' ...,
0.'. "ot ...,
1,1,2,2-
'.,ncllloro
.,hon.
uti'
NI
II U
'_I. or Vo'.' tI.
S U V
S U V
5 U "
II U V
. U
5 U
received
roc. Iv..
ne. I....
rec.lved
.~::.. .-
volatile
surtaoe Water
organio ea.pling
'oluen.
Uti'
Ch'.r.
.........
.,1'
1'10..1
.........
.,,,
..
I U
r."...o''''.
I U "
I U "
I U "
I U "
IU
I U
..
I U
I U "
I U "
I U "
II U "
I U
I U
Results
$I ..r.".
.,,,
III
IU
I U "
I U "
I U
II U "
I U
I U
,.,.,
a..,.....
.,,,
..
I U
I U "
I U "
IU
I U "
IU
I U
.
.
-.-.-
III
2..
Or.."Ie "...1"0'0 ...,
I U "
2.. "
II U "
II U "
I U
I U
V"lU[ QU"llfl[A5: NA - ""olr'. "0' r.por'.d U - A"o'r..d but "0' ..,.e'..
J . 'r...n' below ~.t.ct'on I'." . . 'r....t 1ft '...r.,.r, .'8"'
0"1" V"llO"IION QU"lfl[AS: (No ..."..'10" "..o"'I.r I..dle.'.. do'. 1000 "0' ...." ""'.0'''.)
. - Ho'.'''' tI- "0' -, 1 . 10"-'" ...1..
N - I.'eh 0"'. "., ,.. IO-I~ r.....
. . I.J.c'.., ,,- "cc.,'o.'. .1'10 "..."'Ie.'Io"o,
-------
- 4;~ ..
Surrace Water
Volatile organic Sa.pling Results
SOUTH WALNUT CRBBIt
1.1-0'- 1.1-0'-
St.,'on 0.'. eta'oro 1.- VI.." ''''er. ...,..".... '.rM. ....- ....-
Nv...r 18.,1.. ..t".". ..u..". '..'.rld. .,,,... CII'.r'" AClt... O...UI.. .,- .,.....
"'/' .../. "'/' "'/' ...,, .../. .../. ..I' ..1'
..----- - --- --- _".0__-- --
$V-05' 07/21/" HI HI HI .. HI - .. .U ..
$V-O!ll OI/tO/" 10 U 10 U 10 U 10 U '.0 U 10 U 1.0 . 1.0 U 1.0 ..
5\1-051 ,,/U/', 50 U " IOU " . J " IOU " a. " UO " II. " al. " al. "
$V - 051 05/11/" 10 U V 10 U V . J " 10 U " I J " 10 U " I. " 8 ~ " I "
$\1-05' 01/01/" 10 U V 10 U , IS v 10 U , I U V 10 U , IU v 8 ~ " . J "
$\1-051 07/11/" 20 U ao U I' J a. u H' 10. 10 . II. I ~
5\1-051 00/01'" Oat. not ,., r.c.'..."
$V. 051 0111'/" 20 U ao U 20 U IOU 10 U 20 U IOU 10 U 10 U
5\1.05. 10/11'" 0.'8 no' ret rice'''.''
5\1.051 11/'5'" D.I. "0' ,a' reca'''.'
5\1.051 11/"'" D." ..0' ..., r.c. "'...
5\1.051 01"5'" 0... not ,., rlc.'...
5\1 .051 "'''''' D... ..0' ,., ..c. "'...
$V-051 OJ,'I/tO Oa'a "01 ,a' rac.t"."
5\1-060 01/21/87 HA HI III .. HI - .. IU ..
$V-OIO II/II'" 10 U 10 U 10 U 10 U .. 10. I. I. I.
5\1-010 0"01'" 10 U 10 U 10 U 10 U 1.0 U 10 . 1.0 . 1.0 . 1.0 U
$V-OIO 0)/ ..,,, 10 U " 10 U V a J " 10 U " . JI " tOu " IU " I. " 'IU "
5\1-0'0 0'/"'" 10 U V 10 U V 10 U " 10 U " 1 JI " 1 ~ " IU " IU " I. "
$V-OIO 05'15'" 10 U V .0 U V 10 U V I' U V I U , 10 U " IU " IU " IU "
$V-OIO 01'''1'' 10 U V 10 U " 10 U V 10 U " I I " 80 U " IU " I. " IU "
$V-OIO 01/011" IOU V 10 U V 10 U ". 80 U " I U " 10 U " IU " I. " IU ,
$V-OIO 07/01/" 10 U " IOU " 10 U " 80 U , II ' 10 U , IU " IU " IU "
$V. 010 00/01/" D... ..0' ,., received
$V. 010 01'11/" D.'. "., ,., ,0CO "'...
5\1-010 01/11/" D.'. ..., ..., .oco'"."
511.010 10'01/01 10 U 10 U 10 U .0 U 5 U 10 U IU . U IU
511.060 11/01/" 0.'. not ,at rlcalvld
5\1-060 11'01/" 0... ..0' r.' rice'"..
5\1-060 "/01/" 0... ..0' ..., rice'"..
$V 060 Ol/U/IO 0.1. "01 r.' ...eat"..
5\1.010 0'/01/10 0.'8 ..01 r.t rlc.t...
5\1-060 OJ/II/IO 0... "0' r.' rlcatv..
511-061 01/22/81 HA HA HA .. HI 1M .. I. ..
V"lU[ QUAll'I..5: .... ""..,.. "., r.....'" U - "".I,..d ..", "., ...,.c,...
J - ,....", ...,.. "o'.e'lo.. ".1' I - ,....", ,,, .......'or, .....,
O"IA VAIIDAIION QUAI'I(A5: INo ...11"."0" 8"."".r I..dle.... d.'. h.. ..0' b.... "."".,.'.)
. - ......". 'I.. ..., .., I .. a."..,.. ..0'"
M . I.'c" .,1'. ..., ,,, 1O-11aS r....
. . ..Joc..dl A. Acco,'."'. .1'" ..,.II.Ic..I."., V - V.,"
.
-------
J' . ~
..,
.
8urface .ater
Volatile orqaDia 8a.pliDq Results
80UTH WALNUT CRBBK
'."'-1.2- 1.2.0.- I.I.I-Ir' Cer"'" Ir- I.I-DI-
S,""O" 0.,. 01<1110'0 ."'oro c.'.r. h'.. ,,,..,, ".".r. c"",.
II_.r S..,I.. ..".". l:"l.r.'.", ..".... I."'U-. ..".... ."'.r'.. ac...,. ..'''.- ,r...-
""I ...'1 . ",'1 _.'1 -./1 u." -1'1 -1/' .."
-.--...- .._--- --...- .-----...-- ..---
IV-056 0"'1'1' IV i u I U .. I V IV .. .. "
IV-Oil "'10'" .. 1.1 V !I.O U 10 U 1.1 U I-I U 10 U 1.0 It 1.0 It
'"-056 01''''" ZSU " UU " ZSU " IIU . IIU " ZSU " IIU " IIU " IIU "
'"-01' 01'"'1' I U " I U " I U " 10 U , . " . J " IIU . I U , IU ,
SW-056 01'0"1' I V " IU " I U v 10 U " . " . J " IIU " IU , IU "
'"-056 0'111'1' 10 U .1 U 10 U 10 U I J . J IIU II U IIU
'"-056 01'0"" 0.,. ..., ,., rice'''..
'"-056 0" 11'" 10 U 10 U 10 U 20 U 10 U 10 U IOU 10 U 10 U
511-056 10'"'" 01'. "0' rl' rle.'".d
511.056 11/15'" 0.,. ..., ,., ....."..
511.056 11'"'" D... ..., ,.1 r... ....
511.056 Ol'lS,IO 0.,. ..0' ,., .... ....
511-056 01'21'10 D... "It ,., rlc.'wl'
511-056 01"1/10 0... ..01 ,., rlcllw.'
SII-060 0"21'81 S U S U S U .. I U 11. .. .. ..
SW-"o 11'"'" I U 10 .U 10 U I U 14. 10 U ,. I.
"'-OtO 01'01/11 III 1.0 U 1.0 U IIU 1.1 U 11.1 IIU I.' U I.' U
SW-"O 01' 'I'" S U V II V . U II IOU " I U II '1 " IIU " IU " IU "
511-"0 01'1"" I U V " " I U " 10 U , I U " JS " IIU , IU " IU ,
SII-"O 01'11'" I U " . " I U " 10 U " II v n " II U " IU " I U "
SII-"O 05'11'" . U v I U V . U II 10 U " I U V 851 " IIU " IU " I U "
511-"0 0"0"1' I U V I " IU V 10 U " . V V .. " IIU , 'U " I U "
SII.OIO 0""'" I U V 1 J " S V v 10 U " I V V 18 " 10 U " IU " IU "
"'-"0 01'01'" 0.,. ..., ,.. r.e.'v..
IV-O'O 0"11'" D.,. ..., ,.1 rece'''I'
SW."O 01'11'" on. ..., ,., rlcllwl'
'"-0'0 10'01'" S U I J S U 10 U I U 21 IOU I U I U
'".010 II,Ot,II 0... "0' r.t rICII".d
'"-0'0 11'01'" 0.,. ..., ,., ,.Ie.'"..
'".010 11'0"" 0.'1 "0' r.t rlell.,l.
'".0.0 OI,n/'O 0... no. ,., ,..cII...
'".010 01'0"'0 0"1 not ,., rlc.I"I.
511.0.0 01'11'" 0... "ot r.t ,.8c81".d
'"-061 0"22'8' S U 5 U S U .. U S U .. .. ..
""LUE QU"LlfIERS: IIA - "...1,.. ..ot "'0"'. V. "".Ir... IIu' ..0' ..,..,..
J - Pr.....t ..10. ..,.ctlO" 11.1' . . Pr.....' I.. '...,.,.r, .1..'
DAtA VAliDAtiON quA"lIAS: (Ho ".Ildetlon qu.I'fler '"dlcet.. d.te h.. no' bel" ".1'..'...)
. . lie...... ,... "0' .., I . I.,...,.. ...Iu.
" . I.,." .p". n.' ... IO."~ r.....
. - ..Ject... A - acc.~'..1e .1" .uI'I.lc.".".a
-------
~.', . M
surraa. .ater
Volatile organia S..pling .Resulta
SOUTH WALNUT CRBBIt
e"-I.J. Oillr- I,I,I-Irl trenl-I.). 4.""10,1-
Sta,'on O.te Ole"loro Irlehloro e..loro c..loro D'c.'oro 1-,....
N"".r ...,I.d prep.... .,..... ",".n8 .'''.11. I....". "0'..0 I._fo.. ...... 1-110..-
u./1 ..,,, , u'" .."I ...,, ...,, ..II ..III ..I'
- .-..-.--- --- .._----- ------ --- .-------
W-05' 07121/17 ItA 10 HII I U .. .. .. .. ..
W-051 "/10/88 5.0 U 5.0 U 5.0 U 1.1 U 11.0 U 5.0 V 1.0 V 10 It 10 It
W-OSI 04/11/.8 zau A 120 A 21 U " IIU II zau " nv A I' V A HV A HV A
511-05' 05/11/11 1 U V 140 " 5 U " I U " I U A IV " IV V II V " II V "
511-051 "/07/11 S U It 110 " 5 U It I U ., I U It I V ., IV " II V V II V "
W-05' 07/11/11 10 U 140 10 U 10 V 10 U 10 U II U MV 10 It
$W.051 "/08/11 08'. ...t r.t ree.t"..
511.051 0./14/11 10 U 10 U 10 U 10 U 10 U 10 U 10 U 20 U 20 U
$W-05' 1°/1./11 0.'. "0' ,e' rec.'v.d
511.051 lilli/II D.'. .0' ,., ree.I.,..
$W-051 12/11/11 D." .0' '0' .oeo h.d
511-051 01/25/80 D.'. ..., ,.' rec.t".d
511.051 01/11/.0 D." "0' ,0' ,.ace'"."
511.051 01/21/.0 D... "0' ,0' rac.e.,.d
'"-060 07121/87 HA IU HII IU .. lilt lilt lilt lilt
W-"O 11/11/87 5 U 15 5 U I U IU 5U IU 10 It 10 It
511-"0 07/01/H 1.0 U 11.1 1.0 U 1.1 U 1.1 U 5.0 U I.' U II U II V
W-"O Oil "/11 5 U V 15 V I U It IV V IU It S V V I U V 10 V V 10 U V
511-"0 OJ/ "/11 s U V II V I U " I U V 'U V IV V IV V 10 U " IOU "
$W-O'O 05/11/18 5 U V JI " 5 U V IU ., I U It I U V IV V 10 V " 10 U ,
W-"O 05/11/11 I U It 20 V 5 U ., I U ., I U A IV ., IU . II U " 10 U ,
511-010 0./08/11 I U V U V 5 U It I U , 5 U A I U ., . U , II V , 10 U ,
511-010 07/"/11 5 U V 1 J A 5 U V I V V I U , 5 V , I U ., 10 V ., 10 V .
511-"0 0810JIII 0... 1101 ,0' .oe. h.d
511-010 08111/11 D... "0' '0' .oco 100'
511.0'0 08/11/" D... ..0' ra. race'v.d
5".000 10/01/.. 5 U 5 U 5 U I V S V 5 U IV IOU 10 U
511-0'0 11/01/.. 00'. "o\ re' received
'".0'0 11/"1" D." "., ,0' r.cel"..
511.060 12/0'/11 D." ..0' ,., ..acelv.d
511.010 Ol/U/'O D.'. ..0' ,., receive"
511.010 01/0./.0 0.'. "0' ,., ..aca'",."
'".010 01/12/'0 0.'. ''0' ,., received
'\1.061 01122/81 HA 6 HA IU NIl lilt .. .. ..
VAIUI QUAII'IIA5, HA - A...",o "0' .o,or'.' U - A...I"O. II..' ..0' 'o'oc'"
J . 'ro....' "'o. 'o'oc"o.. "." . . "0..'" ,.. '."oro'.., ..I....
DAIA "AIIDAIION QUA,'IIA5: 1"0 y."..'lo.. ~...I'f'.. ',,'Ie.'.. d.'. ".. ..0' ..... w.l,e.,..-)
. . HoI.I.I 'I.. "0' .., I . I."..,.. w.l..o
N . '.'ell ."'0 ..0' ,.. 8O-llai r....
1I.lIoJ."..1 A. A...,'.III. .".. ...."fl...I....; V - '01"
-------
. J' ,..
,.,
surfaa. .ater
Volatile organia s..plinC) Results
SOUTH WALNUT CRBBK
fe,ra 1.1.'.'-
5'."on 0.'. c"10ro '.'ncIII.;. Clliero It., I '0..1
II-er '_I.. e'''a... .,,,... 101...". ....... ....... It rr.". .,1....
..,/1 "81' ..." ...'1 ...'1 ...'1 ...'1
.--.---. ....--- --- ...------
'".OU 0'121/" 12 1111 NIl NIl NIl NIl NIl
SII. 0!18 01/10'" !t.0 U !t.0 U !t.0 U '.0 v '.0 v '.0 U 1.0 V
III.OU 0"11/" 190 ZlU A nu A ZlU A ZlU A 25U " IIU "
'".051 OIl ..,.. 200 . U " 'U A . U " . U A 'U " IU "
'".05. 01/01'" 110 " I U " 5 U " I U " I U " S U " IV "
,".058 011"'" 280 10 U 10 U 10 U 10 U 10 U IIU
'".051 0"0"" 0.,. n.' ,., r.c.'ve.
'".0'1 0" ..,.. 10 U 10 U 10 U 10 U 10 U 10 U 10 U
'".011 101 ..,.. 0.'. no' ..e. rece'yed
'".058 "'''''' 0.,. .., ,., recat"eel
'11.058 "'''''' 0... ''0' ,., r.c.'"ed
,11.05. Ol/U,'O 0... ''0' ,., rec.t".d
'".058 02/"'10 0.,. n.' ,., r.ca'".eI
'"-Oil 01/""0 0... no' ,., rec.t".eI
511.060 01/'1'81 5U HA HA ... H' NIl ..
IV-OIO "'''''' I U 5 U .. I U I U 5 U IU
IV-O'O 01'01'" 10.. 5.0 U 5.0 U I.' U I.' U '.0 U I.' U
'"-0'0 01'''''' I' " S U II I J " I U " I U " S U " I U "
'",010 OJ,"," " " S U " 'U " I U " I U " 5 U " I U "
'".0'0 05' ",.. IS " 5 U " 5 U " I U " I U " 5 U " I U "
'".010 05/"'" 21 II 5 U " 5 U " I U " IU A 5 U " I U II
"'.010 OliO"" I' II 5 U " 5 U A I U " I U " I U " I V II
'".010 01'01'" 1 J " I V II 5 U II IU " IV " IV " IU "
'".0'0 08/01'" 0.,. .oo, ,., r.u",.
'".010 0'1"'" 0.,. .., ,., r.ul...
'".010 0""'" 0.,. no' ,., ..ul....
'".010 10/01'" 5 U 5 U 5 U IU 5 U 1 U I U
'".010 .. 101'" 0.'. not r.t rec.'ve.
'",010 ",ot,.. 0.,. no' ,., ree.'".d
'".010 "/01'" 0... not ,., rec.t".eI
'".010 01/''''0 D.'. no' ,., r.c.t"e.
'",010 0"0"'0 01'. no' ,., racetved
'".010 OJ, ""0 01'. no' ,., rae.tvad
511.061 01'''/81 5 U HA HA "' III III ..
VAlut QUAII,.tA': HA - An.I". no' r.por',. U - An.I,... ,"w' '0' ...,.C,...
J - 'r..en' ~.,o. de'.c,'on ,.-" . - .r...~' ,. 'a",.'er. .'e'"
DA1A VAIIOA11ON QUAlfIIWS: 1"0 v.".., tOft q..a'I'ta, Indl'.'.. data hI' "0' b.." ".tt...e..)
- - HoI"I.. 'I.. '0' .., 1 - 1.'1..,... ...1...
M - '.'c. ..'te na' 'n 8O-"oa r....
. . ..J.c..., A. Acca,t.... .1.. .w.'lflcl'taRI;
.
" - Vo""
-------
t~ ...
8urface Water
Volatile organic 8a.pling Results
80UTH WALNUT CRBBIt
1.1-0'- 1.1-0'-
5,.'ton Oe'. (hlo,.o 'r- Vln,I '''I.r. ""'" I.... C.r". e"t.. e.'-
II-er 5...... ..'h.". ..,...... ,,,I..ld. .,,,... nt.rt.. Ac.'.". Oh."I" .,.... .,.....
..,/I ..,I' ..,/1 ",'1 ..,t ...'1 ..'1 ",'1 .1/1
. -. u. - -----.-- ----.- -.. ------ ----- .---
$IW-HI 11/11/11 10 U lO'U 10 U 10 U 10 10 U IU IU IU
$IW-HI 0"01'" 10 U 10 U 10 U .. U 1.0 U 10.U I.' V I.' U I.' .
$V-HI 01/10/11 0... "., ,., r.c.tw..
SW-HI 05/15/11 10 U V 10 U v Z J A 10 U V II U V 10 U V IU V IU V IU V
$V-HI 0'/0'/" 10 U V 10 U V '" " 10 U " IU " 1 "I" IV " IU " I" "
$IW-HI 0"0'/11 10 U V 10 U V ... " 10 U " '" " 10 U " IU " IU " '" "
$V-H' 0'/01/11 .... "., ,., r.c.lv..
$V-HI 0./11/11 .... "., ,., r.c.lv..
$V-HI 10/01/" 10 U 10 U 10 U 10 U . 1 10 U I U IU IU
5".HI 10/20'" 011'
5"-011 11/01/11 0.'. no' ro' roco t v.d
5\1-061 12/01/11 0.'. ..t ,., rec.t"o"
$V-HI Ol/ZI/'O D.'. no' ,., r.c.'"e"
SW - Oil 02/0'/'0 D.'. not ,., rec.I"e'
5"- 061 01/11/'0 D... ".1 ,., rec.I"eet
5\1.061 01/12/'0 0.'. ''0' ,., racetv."
5\1-101 01/10/88 10 U 10 U 10 U .0 U 1.0 U 10 U I.' U 1.0 U 1.0 U
$W-IOI 0./ IJ/II Det. not rot rece'v.d
$V-IOI 05/11/11 10 U v 10 U v 10 U V 10 U " I" A 10 U " IU " I U " I U "
5"-101 0./01/.. 10 U " 10 U " 10 U " 10 U " . U " 10 U " IV " IU " I V "
$V-IOI 01/11'" 10 U 10 U 10 U 10 U '" 10 U IU IU IU
$V-IOI 08/0"" 10 U v 10 U v 10 U v 10 U v 1 .I, A .. " I U " IU " I U "
5"-101 0'/1'/" 10 U 10 U 10 U 10 U . "I 10 U I U I U I U
5"-101 10/11/11 ..,. "., r.' r.cetv..
5\1-101 11'15/11 0.,. "., ,., r.c.lv..
SW-iol IZ/II/II 0.'. "., ,., r.c.I"..
$V-IOI Ol/U/.O 0... "., ,., ..c. h..
5\1-101 02/22/10 0... "., ,., ..c.h.d
5"-101 01/21/'0 0... "., ..., rocelv..
VAIV( QUAllfl[AS: HA - 41".1". "., r.por'.d U . A".I,..d ..., "., "'.e'"
J - 'r...,,' ..10. ...tactton It.tt . . 'r...nt .. '."r...r, ~,...
OAIA VAIIOAIION QUA\fIIAS: (110 v.II.., 10" qv."'I.r 'nd'c.'.. d.'. ... ..0' b.." ..'1..'...)
- . ...1.1.1 ,... ".. .., . . ..'1..,.. ..,..
.. . '.'c. .,11. ..., I. IO-IIGS r....
. . '.J.c,..\ A. Ac..p'..'. .1'. ....1.,...'10".; v - v.I"
,
-------
J,.~ ow
.
.
Sur race Water
Volatile organic S..pling Results
SOUTH WALNUT CRBBK
,...1-1,'- 1.2.0.- '.I.I-Irl C.rlt... Ir- 1.'-01.
Stet ton Oet. O""Ioro c"I.r. ..1.,. Ye',. "I." ..c.,-. ..,-
"_., ,...,.. .,...". '''I.r.'." .u..... '-1.'.-.. .,...... c..,.,I.. ac..... ....... .,......
u./I .." u,'1 .." -,'1 .." -." ..'1 ..'I
--..---- ----- - . ---.-- --
Sill-OIl ..,..,., 1 U II 1 U 10 U IU , II U IU IU
~ IV-OIl 0'/01'" ... 1.0 U 1.0 U I' U S.. U ,.. II U 1.1 U I.' U
IV.OII 01"0'" o.t. ..., ,.., roC. I"...
Sill-OIl 0" 15'" 1 U " I J " I U . 10 U . . " 22 . 10 U " IU " IU "
IV.OII 01'0"" I U . I J " I U . IIU " I U . II " '1. , IU " IU WI
IV-HI 0"01'" I U " 'J " I U ., 10 U . I U " , . II U , IU " I U "
'''-011 O"OI'~' 0.'. ftO' r.t r.cet"...
Sill-HI 0""'" 0.,. .... ,., rec.t"..
'''-HI 10/01'" I U I J IU 10 U I U II 10 U IU I U
IV-OIl 10/'0'" DIIf
$W-OII "/01'" 0... not ..., rece'".d
$W-OII "'01'" 0... ..., ,.. r.c.I"..
$W-OII 01/'1'10 on. .... ,., ,...1"..
Sill-OIl 0"0"10 D... ..., ,.. r.cet".d
Sill-HI 01''''10 0... ..0' ,.. ,... I "..
Sill-OIl 01' "'10 0... ..., ,.. recet..d
$W-IOI 0"'0'" "" 11 1.0 U I' U 1.0 U 1.0 U II U 1.0 U 1.0 U
Sill-10 I 01' U,.. 0... "0' ,.. r.c.t"...
SiII-IOI 0" ../.. I U " II " 1 U . 10 U V 1 U . 1 U . 10 U . 'J " IU .
SW- '01 01'0"1' . U " II V S U . II U " IU " I U . IIU " ... " IU "
SiII-IOI 0""'" I U " S U IIU I U I U IIU . .. I U
SW-IOI 08'0"" I U " " V S U " 10 U . . U " I U . .0 U . . J " IU .
Sill-10 I 0" "'" I U II I U 10 U I U S U II U I J IU
Sill-10 I 10' ..,.. 0.,. ..., r.' roc.t"..
Sill. 101 .., "'" D... .... r.. ree.t....
SW-IOI ",It,I. 0... ..0' r.' roc.t....
'''.101 01'15'10 0... ..0' r.' recet".d
.,,- 101 02'22'10 D... "0' ,.. rec.t...
'''-101 01''''10 D... ..0' r.' rec.I".'
VAlUl QUAllflllS. HI. .".1,.,. .0' r.port.. U . An81,.... .., .., '.'ec'"
J . 'r...... ".Iow ....c..... II.'. I . 'r.....' ... ,...,..." .1...
DA'A VAIIDA'ION QUAI'IIIIS, ("0 ..".."0" qu.I.f'.r 'n.'e.... .... ".. "0' ..... ".11......»
. . M81.... e... ... .., I - I.tt..,.. .81.-
" . ..te" .".. .... ... 1O-11Oa ,...,.
. . I.J.C'..I A. Ace.,'."I. w'," ,..'I'le..'.",:
-------
~..~ . ~
surfaae Water
Volatile organia ...plinCJ Resulte
SOUTH WALNUT CRBBK
Ch-I.I- Dlbr- I.I.I-Irl lre",-I.I- .-......,1-
Stet ton Oat. Dlchloro Irlcltloro c"'or. c"l.r. Dlcltloro I-po..'.
II-.r .,..Ied prop.". ....... ..."... .,,,... ........ ,ra,.". 1..-'... .... .-.........
MI/I ../1 u./I ulll ..,, u,/1 ..II ../1 ..I'
. _u.-- -..-- - -- -.--- -- ---.---
5'0-081 II/II'" 1 U '0 1 U I U IU $ U I U 10 U 10 U
W.081 0"01'" 1.0 U $.0 U 1.0 U 1.0 U I.' U 1.0 U I.'. II. ...
1\1.011 01/10/1. Do" "0' ,., r.C. .....
SV-OII 01' ..,.. 1 U . II V I U . I U , IU V I U , IU , 10 U V 10 U ,
1\1.011 01'0"" I U , " ' I U V I U , I U " IU , IU " .. U " .. U ,
SV -011 0"01'" IU , 1 J " $ U V I U , IU , I U , I U " IIU " '0 U .
SV. Oil 08/01'" Do.. "0' ,., r.c."."
SV.OII 0""'" 0... ".. r.' rec.t"..
1\1.081 10'01'" 1 U 1 U 1 U I U I U 1 U 1 U 10 U 10 U
sv-OII 10"0'" IltU
SV. 011 "'01/" Doh 110' ,.. r.c.tv.d
SV-OII II '01'" D... II.' ,.. r.e.t"..
SV-OII ol,n,.. Do.. "0' ,.. r.e.t"..
SW-OII 0"01/10 De.. "0' ,.. recetv.d
$V-Oil OI,U/IO D... "0' ,.. r.c.tved
SW -011 Ol/U/.. D.'. "01 ,.. recel".'
SW-IOI 01'10/81 1.0 U 1.0 U 1.0 U I.. U I.. U $.0 U I.' U .. U 10 U
W.IOI 0.' 11'" Do.. "0' ,.. rec."."
1\1- 101 01/ "'" I U V I V I U , I U " I U " 1 U V 1 U " .0 U " 10 U V
SV.IOI 01/0"" I U V S u V IU " IU " IU " IU " I. " .. U " ... "
SII.IOI O"U,.. I U I U I U IU IU $ U I. .0 U .0 U
1\1.101 0'/0'/" I U . S U . I U . I U V IU " I U , IU , IIU , 10 U ,
1\1- 101 0"1./" I U I U I U I U I U I U I U .. U .. U
$V. 101 10' ..,.. De.. "0' r.' rece'va'
SV-IOI "'''''' De.. 110. ,., r.c.I.."
SV- 101 12'''''' Oa'. ..0' ,.. r.c.'v.'
SW.IOI 01'11'" D... ..0' ,.. rec.'v.d
SW.IOI O"U'IO 0... "0' r.. r.c.'vad
SW-IOI 01/"'" 0.'. ..01 ,.. r.cetvad
."LU( QUALlfl(RS: NR. A...I,.. .... r.por... U . A...I".. "u. II.' ..........
J. 'r...... '.Iow ..'.C"Oft ,.... . . 'r....' ,. '.'.r...r, .,...
0"'" .ALIDA.ION QUA.'I(RS: INo ..11...10.. qu.II'I.r 1...1...., d... ..., "0' ...... ..II..,...t
. - """1.. tt- .... -. I . 1.,,_,... ...1-
II. I.'d '.'.. ..., ." 80-11- r....
. . ..J...... ". A...."..I. .1... .u.'I'I.....",.
" . V.II..
-------
J' ...
..,
Surfaae .ater
Volatile organia S..pling R.sults
SOUTH WALNUT CRBBa
'.tr. 1.1.2.2- .
5'."0" D... c"loro '.,ree"l.r. '''I... 1,,,,1 '.'.1
II_a. Sa.. I.' .t...". .,..... 101.,0". ....- ........ S',n... .,Ie...
.../1 ,,"1 .../1 ../1 ../1 ../1 ,,"1
.-.-------- -.----
N-061 11/11/.7 au I U II I U IU au IU
N-061 07/01/.. 1.0 U 1.0 U 1.0 U I.' U I.' U 1.0 U I.' U
511-011 OJ/IO/" o.t. ..., ,., roc.t"o.
N-OII 05/15/.. 10 " I U " I U " I U , I U , IU , I U ,
51/.011 06/0"" " " I U , I U " I U " IU " I U " IU "
$11-081 07/08/" , J " 1 U , 5 U , 1 U , IU , 5 U , IU "
511-081 OI/OJ/.. 0.,. no' ,.t roc.t"..
511.011 0"11/" 0... ..., ,., rec.tv..
511.011 10/01/11 I J 1 U S U I U IU 1 U IU
511.081 10/10/8. [III,
511-081 ../08/.. 0... no. r.' r.cel"o.
511-081 II/HI" D... .... ,.. ree.'..'
511-081 Ol/IJ/'O D.'. ..., ,., ..c.'..'
511.081 0110"'0 0... ..0' ,., r.c.l"o'
$11-011 OI/U/IO 0... ..0' ,., roc.'w.'
$11-011 OJ/ U/IO 0... ..., ,., .ec.au..
511-101 06/J0/88 1.0 U 5.0 U 1.0 U 1.0 U 1.0 U 1.0 U I.' U
511-101 ot/ll/" 0.,. ..0' ,.. roc.S.o.
$11-101 05/11/" It " 5 U " t J A I U " 5 U A IU " IU "
511-101 08/07/.. I U " 1 U " I U " . U , I U , 1 U , 'U "
$11-101 07/U/" 1 U I U I U 1 U I U I U IU
511-101 08/0"" I U " I U " $ U A I U " I U A I U " IU A
511-101 O"lt/ll , J I U 1 U I U 5 U I U IU
511-101 10/11/" 0.'. "01 ,ot rec.t...
511-101 11/15/11 D.'. ..., ,., .ec.au..
511-101 U/"/II 0... ..., ,.1 rec.lv..
511.101 01/25/.0 0... ..0' ,., rec.I...
511-101 01/21/10 0.'. not ,., r.c.lw.'
511-101 OJ/ll/lO D.'. not ,., r.c.lw.'
"AIUE QUAllfIEAS: "A. A...I". ..0' ..po.'.' U . A...I,... but ..., '.'.c'.'
J . Pr...,,' ..10. ..'.ctloft ,.... . . 're.en' 1ft I."r...r, ~I..'
OAIA VAL IDAI ION QUAlfIEA5: ("0...1"."0" 8...1"'.. ',,"e.'.. ..,. h" "0' b.... ..It'.'.'.1
. - "''''''' It- ..ot _t I - hlt-'" ...1..
II . '.'e" 8"'. ..., t.. 80-1101 r....
. - a.Joe'.'1 A - Ace.,'oll'. w"" ,...It.te.tt...o, ,,- "..t.
-------
~,~ ...
Volatile
surface Water
organic sa.pling
Results
STATION 59
I.I-D'- 1.1-0'.
5'."0" 0.'. Chloro 1.- V"'r' "'.... """1".". c...." ........ ....-
"-.r s...'." -,...... -,...". C.....I... .,...". "'.r'" "c...... 0"."'.. .,..... .,.....
"I" "I" "I" "I" .1" ...,, .,1' ...,. ..'I
--...---- -------
W-OSI 0""'" \III \III \III \III \III \III . III .
W.OII 0'/01'" 10 U 10 U '0 U 10 U 1-0 V 10 V I.D . 1.1 V 1.0 .
$\I-OS' 01/'0'" SO U v IOU V SO U v IOU " "JI" 10 U " IIV " I~ " ... "
$\I-Oil OS'''''' IOU " IOU " 10 U " IOU " 1 J " 10 U " HU " 'J , . ~ ,
$\I-OSI 01'01'" 10 U " 10 V " .0 U " 10 U " I JI " 1 ~ " IV " I ~ " I J "
$\I-Oil 0"01'" 10 V " 10 U " 10 U v 10 V " I I " "I " IV " .~ " I ~ "
$\I - Oil 01/10'" 08'. ".. r.t r.c. h..
$\I-Oil 0'/11'" 10 U 10 U 10 U 10 U . JI 1 JI 1 U I J , J
$\I-OS' 10'0"" 10 U 10 U 10 V II V . V 10 V IV .~ IV
$\I-Oil "'01'" 08.. "ot ,et rec.t.,.4
$\I-OS' "'01'" D... ".. .... ..c.h.'
$\I-Oil O',U,IO 0.'. ".. .... ..c.h.'
SW-OII 01/0"'0 o.t. "01 .... rec.h..
SW-OII 01'''''0 0... ".. 1'.' rec.'".'
V"lUi QU"llfl[AS: "A. "n.'r'. no' r.por'.' U . "n.'r... .... ".. ...oc...
J. Pr.,.ft' ..10. ..,.ct.Oft I.." . . 'r.'.Rt .. ....r.'.r, .....
0"1" V'"10"1 ION QUAlf'IAS: ("0 "."".'I.n q"."".r '"dlc.'.. d.'. .... no' b.." "."..'.'.)
. - ...,..., .... ".. ... I - I......... ......
. . t..c" ."... n.' I. 10-11" .....
. - a.J.c'.', ". "cc.p..". .... .".'...c.,.o..; V. ".,..
-------
. ~.~ .-
.
.
Volatile
8urfaae Water
orgaDia .a.pling
Re.ults
.'1'&'1'IOH 5'
"'.1-1.2- 1.2-01- ......fr' Clr... 'r- ..I-DI-
Stet'on 0... Oh..ln. ."'.r. ... .er. f.'r. ....,1 ,"eII'.r. ...-
II-.r S...I... .'''.ft. C"'.r.'." .'''.n. 1-"'.- .,..... c.'.r". ...tn. ........ ........
..,/1 .'/' ..,/1 ../. .,/1 .,/1 "'/' ../. ..I'
.---- .----- ----
"-OS' 0'/"/" IU co 1 U .. IU 101 .. .. ..
"-011 0'/01/" .. ".J 1.0 U '0 U I.. .., 10 U 1.0 II 1.0 U
III.OSI 01"0"1 2IU V 8Z v lSU v "U v 41 II ..0 V "U . II U v IIU "
III-Oil 01' II'" ISU v I' v nu . IOU . II ' 110 "U . IIU . IIU ,
"-OSI 01/01/.. I U , 10 " I U , .0 U . II ' 100 ' '0 U . IU . IU ,
"-011 OJ/OI,,, SI . " ' I U , '0 U . 10 ' .10 . .. U , IU . IU ,
$V-OSI 08/10/.. De,. nDt ret rec.I"."
$V.OII 01'''''' I U II 1 U '0 U I 1'0 10 U IU S U
"-OSI 10/01/" s U IS S U .. U I U "0 .. U IU IU
SII-OSI "/01'" 08.. n0' ,., rec.h...
$11-01' 11'01'" 08.. ..., ,., r.c.I...'
1II.0n 01'21'10 00'. ..., ret rec.t...
"-OSI OI/O',tO 00.. ..., ,., r.ul.....
$V-OSI Ol/"/tO 00.. no. ,.. r.ul....
VALUE QUAllfIIAS: H~ - Aft8'r'. ftot report.d U - Aft.'rled ~yt ftO' ~.,.c...
J . 're..,,' ..10. 4.,.ct'on .t.8' , . 'r....' In '."rotor. ~,..,
OlllA "AI 10111 ION QUlllfllA5: (No ..11".'1010 q..."fl.r In"le.I.' d.'. .... no' b.... ...II.......t
. - ""~t... t'- ..01 ... 1- 1.,.-,.. .,.,...
II. I.'e. .~I.. 10.' In ID-ilal r..,.
. . '.J.c,.., A. "ce.,'..'. .1'" ....II"c."o,,",
-------
8TATION 59
(II-I.J-
St., 1o" O.t. Olc"loro hlchl.r.
lI""u S..,lod ,r.,.... .,tI...
..,'I .."I
---..-.---
$W-on OJ ,,,,,, .. IZ
$W.OI' OJ "1'" 5.0 V .,
$W.os. 01"0'" ZlV V 210 V
$W.on 01'''''' uv V .80 "
$W.on ..,..,.. I V " 10 "
$W. on OJ'''''' I V v II "
"'-011 0"10'" Dot. ..0' ,.. roc. h...
"'.011 0" ..,.. I V II
$W.OII 10'01'" . V 12
111.05. ..,",.. 0.'. "01 ret rec.tveet
$W.05. .,,",.. 0... .... ,.. r.c.I..'
511.011 OI'U,'O D.'. .... ,.. r.c. h..
511.05. OI'Ot,tO 0.1. .... r.' rlc.'",.
511.05' 0)''''10 0... ..0' r.t rlce.".d
. .~~ ...
8urf.a. ..t;.r
Volat;ile organic ...pling R..ult;.
Dlbr- ...,I-'rt Ir....-" J- t-......,. -
c".ro clll.r. Olctl'.ro 1-...'.
..III.... ..".... ....... ".,.... er-.... .... 1-"'..-
.../1 ../1 ..I a ..1' ..I' .,/a ..,.
-----
HII I V .. .. .. .. ..
5.0 V ... V 1.0 V 1.0 V 1.0 V .0 U ao..
25V V IIU " IIV A nv II IIV " "U " .... "
ISV " IS V " UV A UV " II V " ..v " ... "
5 V V I V . IV V 5V " I V " .8 V " .8 II "
I U V I U " I V A I U " I U " .8 V . .8 U .
5 U 5 V I V 5 V . V 10 U 10 U
I U IV I V IV IV .8 V .0 II
. . NoI.I., .1.. ...t ... . - ...1..,.. ...1..
II . '..cll .,1.. .... I.. 8O-.~ r....
. - ..Ject.., A - .cc..t.~'. w.,. ~u.'t"c."Oft'&
VAtU( QUALlflfAS: HR - A....,.. ..0' r.por'." U . An.I"., b.. .... '...c..'
J . .r.,...t ..loM _.'Ie,'oft ...., . . 'r.....' 'A ',"r.t.r, "...
DAtA VAtlDAtlON QUAt' liAS; (Ho "..,...10" qw."f'.r Indlc.'.. de.. h.. ftO~ b.i.. ..,...,...)
V - V.""
-------
~.', ...
surfaae Water
Volatile organia Sa. pIing aesults
STATION 59
'.tre 1,1.','-
St.t'on O.t. d.loro ..tnc"ler. '''.r. ..",I .....
_er ,...1... .'''.n8 .,...... 101...... ....... ....... $t,n.. .,.....
..,/1 .../1 I .../. .../. ...,, .../. ...1'
- - - ."'--.- .~. _. ~ ._- ----
$V-ost 01/11 /., 10 '.. N' .. .. .. "
$V-on 01/0./.. ., 1.0 U 1.0 U 1.0 V 1.0 U 1.0 U 1.0 V
sw-on 01/'0/" 210 v IIU v ZlU A .1 U " IIU " IIU " II U "
swoon 05/11/" 110 v IIU . ZlU " IIU " IIU " IIU " IIU "
sw.ost 01/0'/" 11 v I U " 5 u . I U v 1 U v IU v IU It
sw.on 01/01/" II v I U " I U " I U " I U " 1 U " IU "
SW-05' 08/10/" De.. ...t ,.. rec.t"..
swoon 0./../" II I U . u 5 U I U 1 U I U
s,,-on 10/0)/" u 'U , U I U IV I U I U
s,,-on II/ot/" Oat. "0' ret r.celved
SW-OII n/OI/" De.. ... ,., ree.t"..
swoon 01/21/.0 D.'. ... ,.t reee'"..
swoon 0'/0'/10 D.'. .... r.' rae.t".'
SW.olI 01/1'/10 0... .... r.t r.e.I".'
VALUE QUAllfIIAS: HA. A"-'r'a no' report.. U - A"-'r,ed ~~, ..ot 4.'.ct.'
~ - 're.a.' ~alo. ..,.c"on I'." . . 'r....' 1ft '...r.tar, ~'.R'
OAI. "AlIOAIIOH QUAlfIIAS: eNo v.II'.'I.n qu.llfl.r 1..'lc.'.. ...,. h.. not b.... ..11'.,...)
. - ~'.'ft' ,... "0' .., . . I.,...,.. ".Iu.
. . '.'ch .pl'. ..., In 80-1101 r....
. . '.J.c'.', .. Ac,.,..." .1'" ~u.llflc.'lo...;
.
.
-------
J" OM
",
surface Water
Volatile organic Sa.pling Results
STATION 63
Stet Ion Dot. Chloro Ir- VI..yl
N-er So.,l.d _tho... _U..... C"lorldo
ui/' "1/' , uilil
___.0__0_-.--'- -------- ----
$W-NI 07/24/87 Nil l1li HA
$V.N. 07/N/.. 10 U 10 U 10 U
$W-OU 01/28/.. DRV
511.0U 0'/12/" DR'
$W-OU N/21/.. DR'
$V.OU 07/11/.. DR'
$W-N' 08/11/.. DR'
sw-OU Ol/!'/" DRY
SW.OU 10/04/.. DRY
511.0U II /01/" DRY
511-N' 12/01/.. OA'
$W-OU 01/0'/110 DRY
SII.OU 02/02/10 DRY
1,1-01- . ,1-01-
C,"'or. ""hr"'" Corbo.. c,"'.ro c'",-
....... CII'orl" Aceton. Ota.1fI... 0'10.... .'10...
u,/I "II' ui/' .1" "1'1 III"~
-- -----
NIl HA .. NIl au NIl
10 U r..0 U 10 U 1.0 U 1.0 U 5.0 U
VALUE QUALlfIEAS: NA - A..olyto ..0' r.port.d U - A..oly..' but ..ot 'o'oc""
J . Pr...nt ~.lo. ..t8ctloft 11.lt . . Pr...ftt tn '.~.r.'.r, ~'.R'
OAIA VALIDATION QUAlfIEA5: (Ho vo'I'otlo" ~..ollflor In'leot.o dote "00 no' "o.n vo'I'oto'.)
. - Holdl., tI- ..0' -, ( - Iotl-"" vo'"o
N - 'otcll opl". ..ot I.. IO-I~ ro..,o
. - A.J.ctod; A - ACcoptob'o wl'h .uo'lflcotlo..o; V - Vo'I"
-------
Volatile
STATION '3
'ohl-I,2- 1.2-01-
5'.'10" De'. Olcilloro ch'oro
M-or S.....od .then. Clle.ro'o", .'h.".
v,ll .../e . u,ll
....-...-- - .----.-- --- -. .._-+----
5'1-061 01/24/81 5 U 5 U 5 U
5'1-061 01/08118 Mil U 5.0 U
swoon 01/28/" 011'
sw-on 05/121" 011'
swoon 0"2e/,, 011'
sw-on 011"'" 011'
sw-on 08/''/'' Oil.
sw-ou O./IS/.. OIl.
SW-OII 10/04/" DAY
SW-OII "/01/" 011'
swoon 12/01/" 011'
5'1-011 01/05/tO 011'
SW-OII 02/02/10 OIlY
~.~ ...
.
Z-'.."..".
.../e
NIl
eo U
VAlU[ QUAlefl[IIS: NIl. A...I,to "ot roport.. U . A..ol,'Od but "ot ..t.ct..
J . 'ro..,,' ..10. .ot.ctlo.. Iialt . . 'ro.o"t I.. eo..r.t.r, .e..,
OAf A VAllOAflOH QUAlfl[AS, (Mo voel..tlo" ~v.'tflor 1".lc.to. do'o .... "ot boo.. v.e'.oto..)
Surface water
organic ...pling
.esults
1,I,I.'r' Carbon 'r-
clt.oro 'etr. VI"" .'clleoro
.tllo". cll'or'.o "c.'at. "'"0..
u8/e .../e u.I' u.I'
-- ---
1 U 1 U NIl NIl
1.0 U I' 10 U 1.0 U
. . ...,.,... tI.. "ot ..t « . htl_t.. vo'v.
M . 'otcll .,1'0 ".t ,,, 1O-IZaI ro...
II - lIoJoctO.1 A. "cco,t...,o w'tll ~v.'lf'c.t'o".; y. voe,.
.
I,I-D'-
ell'or.
,......
...,,
NIl
-------
. ~.~ ...
Volatile
8urface Water
organic 8a.pling
8TATIOH 63
'h-I.J- OtbrOMO 1.1.'-'rI
5..tlon Date Dlehloro 'rleloloro c"1oro e"lor.
H"".r 50....41 propen. .,...... ......... .,,,.... ......".
u,/I .,/1 I .,/1 u,'1 .".
'.'---- ----- -- --- .-----
w-on 01/24/11 NIl II U "R II U NIl
W-OII 01/01'" !I.O U 14 !I.o U 11.0 U 5.0 U
W-OII 01/21/11 l1li.
W-OII 05/1"" l1li,
511-011 01/21/11 l1li,
511.011 01/1"" l1li.
511.011 08/11'" l1li.
$V-OIl 0./15/11 l1li'
$V-OIl 10/04'" l1li'
511-061 11/01'" DAY
511-011 12/01/" l1li'
511-061 01'05"0 l1li,
511-06) 02/02"0 l1li'
Results
Ir.nl-I.J...
Dle"loro
pro,....
.,/1
l1li
5.0 U
Ir_f...
.1/'
..
11.0 U
4-""'''1''-
.-,..,.
.....
..,/1
1M
10 U
VALUE QUALifiERS: "A. A"ol". "., r.,o.'.d U . A"ol,..d ~t "., ...'OC''''
J - .r..."t ..10. ..,.ctton 1'.1' . . Pr.....t ,,, '...r.'.r, .....
OAIA VAllOAIION QUlllf1EA5: CNo v.I'do"o" ~.."f'.r '"d'eo'.o d.'. "00 not boi" v."d.'.d.)
. . Mold'.. 'I.. "ot ..t 1 . I."..,... ...1...
M . I.'e" .,.,. "., ,,, 1O-IZGa r.....
. . ..J.e'.d. A. Aee.,'o.l. w"" .u.I'f'eo"."o.
., . .,.....
.
'-Mo....".
../.
NIl
10 U
-------
STATION 63
tetra '.',2,2,
St.,'on O.t. cllloro "'rullloro
M_or So..Io. .t".... ."'..0
u./I .,/1 ,
----- --
$V-on 07/21/.7 1 U l1li
W-OII 07/01/" '.0 .. 1.0 U
S\I-OII 0)/28/.. 011'
S\I-OI) 05/12/.' 011'
5\1-011 1It/"/.' 011'
S\I.OII 07/../.. 011'
S\I-IIt) 01/../.' 011'
5\1-01) 0'/15/" 011'
5\1-IIt) 10/01/.' 011'
$V-OI) . ./01/.' 011'
5\1-01) 82/0./.' 011'
5\1-1It1 01/05/10 DII'
5\1-01) 02/021'0 011'
Volatile
loluen.
."1
..-----
J' ...
",
surfaoe .ater
organio Sa.pling
'"I.r.
.........
.,/1
l1li
1.0 U
'ALU( QUALifiERS: MA - A.olrt. .ot r.,ort.. U - A.olr..d ~.t .., ..toct..
.. - 'r....' ..1.. do,oc,Io. It.t' . . 'r.o..' I. 'o~r.'.r, ~Io.'
00'0 'ALloo'ION QUolfiIAS: INo voltdotto. ~..olt't.r 'ndtcot.. dO'o 110' .ot ..... ...Itdo'ed..
HA
5.0 U
Results
1,",1
~......o
.,/1
S',ro.o
.,/1
ItA
1.0 U
ItA
1.0 U
.
'.'.1
I,.....
.tI'
..
1.0 U
. - 1Io'.t., tt.. ..ot .., I - lott..,.. ...,..
" - '.'cll .,t.o no' t. IO-IIGS ro...
-------
Volatile
STATION 6.
Stl'ton 0.,. Chloro 'r- Vlnrl
II-er S..,I.d _tha". -,...". C,,'ortd.
u,/' "'/' , "1/'
------ --.--.-
$W-0'4 07/22/87 till IIA 1111
$V-0I4 0'/07/" 10 U 10 U 10 U
$W-O" OJ/IO/II OR'
$V-O" OS/22/" 10 U v 10 U V 10 U V
$V-0I4 01/"/11 10 U V 10 U V 10 U V
$V-0I4 0'/11/8' OR.
$V-0I4 08/11/8. OR'
$V-O" 0./20/8. OR'
$V-O" 10/04/11 OR'
$V-0'4 11/0./11 OR'
$V-O" U/OI/II OR'
SW-O" 01/05/.0 OR'
$V-O" 02/02/.0 OR'
.' .-
",
surface water
organic sa.pling
Results
I,I-DI- '.1-01-
C"Ior. ...,,,,1.". C.r~- ell'.". ell'.'"
.,,,.... elll.r'" Aceton. Dh.'"'' .,".". .,.....
../1 "'/' .'/' ..1' ..I' ..11
-- _._-
till till till till IU till
10 U , U 10 U I U IU IIU
10 U V .. A Z.J " II U V II U V II U V
.. U V I U V II J " . V I U V IU V
VALUE QUALifiERS, 1111 - A".'". "0' r.,or,.d U - An.lr..d ~., "0' ..'oc,..
J - 'r...,,' 108'.. '.'.c'Ion 11.1' I . Pr.....' I.. ',"'r.'.r, ",...t
DAIA VALIDA'ION QUAI'IEIIS: (11o v.'I'.'lon q..lt".r Indle.'.. d.'. ".. noC ..." v.II..C...t
. . tIol'I". CI- noC _C ( . (.CI_c.' ...1..
II . I.'ell .,It. "., In 1O.la~ r.....
. - '.J.c'.., A - Ace.,'.b'. .1" 4..'I'Ie.'I.n., V. V.II.
"
-------
~.~ ,.
Surface Water
Volatile organic sa.pling Results
STATION 6.
10&81-1,2- 1.2-01-
St.tlo" Ott. DIe"lo.o eta'oro
N"'.r 50....lod ethe... ''''0.0'0.... et".". I-...to.o...
.../1 .'/' ' .../1 ..1'
---.-.--- _..---- -- -----. .-..--
$\1-014 07/22/.7 SU I U S u HI
$\1-014 07/0'/" HI s U S U 10 U
SW-0I4 OJ/JII/., III1Y
511-014 OS/22/" 5 U Y 2' Y I U Y 10 U Y
511-014 0./27/.' I U Y I J " S U V 10 U .
511-064 0""'" 1111'
SW-Ou 0"11/" III1Y
511- 014 °"20/" 1111'
SW-O" 10/04/" 1111'
SW - 014 11'0"" 1111'
511-014 12/01/" 1111'
511-064 01/05/10 1111'
511-0" 02/02/10 1111'
VAlU[ QUAllflfR5, HR - A"o','. ''0' .opo.'od U - A"ol,.od "..t "ot .otocto.
J - 'r.....t ..'0. ..t.ctlon 'I.lt . . 'r...ftt 1ft '...reter, .'.a.
DAIA VAIIDA'ION QUAI'I[RS, (Ho vo'ldo"o" q..o'I"o. '"dlco'o. dO'o "0. "ot boo" vo'I..'o..)
1,1,1.'.,
C"'o.o
.."....
.../1
C.rboft
'otr.
c"'or'.o
..,"
--
I U
I U
I U
I U
I U v
I U Y
J J "
5 U ¥
y,.."
Ac.'o'o
.../1
HI
10 U
10 U V
10 U ¥
T
Ir-
.lIe"lor.
_'''0-
.../1
HI
S U
I U Y
. U ¥
. . ......., t I.. "01 .., I . 18t I_t.~ wa 'u.
N - lo'c" .,1'. ..ot I.. '0-12ak ro...o
. . RoJoc'odl A - Accopto"'o .It.. q...'I'lco'lo".1
II - Y.II.
~
I,I-DI-
."10'"
"'''..0
...,,
HI
I U
S U II
-------
8urface Water
Volatile organic 8a.pling Results
8TATION ,.
CII-I.J- Olb~o.o I.I.I-'~I
5t.'lon o.u Ole" lo~o '~le"lo~o ch'oro elll.r.
"_or 5....1.. propane .,"... _t".... .,,,....
u./l ...'1 . u./l u.,1
---------- ..----.- -----------
SW-Ou 07/22/87 ... 20 HII I U
SW-CHI. 07/07/.. 5 U I U 5 U I U
$W-OU Ol/JO,,, OIlY
SW-O'. OS/22/" 5 U v I' v 5 U v II U V
$W-CHI. 06/21/" I U v II A II U v I U V
$W-064 07/"'.' OIlY
SW-064 08/11/8' OIlY
SW - 064 0'/20/" OIlY
$W-064 10/0.'" OIlY
$W-064 II '0"8' OIlY
SW-064 12'01/8' DAY
SW - 064 01'05"0 Dill
SW-064 02'02"0 OIlY
VAlUI QUAI If liAS: HA. A...I,t. ..ot r.port.' U. A...I,... but ..., ..'.e'.'
J - Pr...n' ~.'OM ..'.Cllo" 1'." . . .r...~t t. '._.reter, .,...
DAIA VAliDAIION QUAIFIIAS: eHo v.II,.tlon ~u.llfl.r In'le.t.. .... .... "0' ...... ...II..t.',)
.......
.../1
""
I U
5 U A
I U A
'ran,-I,).
Oleilloro
,ro,....
u,/1
H"
5 U
II U .,
I U .,
Ir_f...
...,.
""
I U
I U v
I U ,
.....,..,1-
I-po...
.0"8
.../1
...
10 U
10 U .,
10 U .
. . .....1.. tI- ..ot -, I . l.tI-'.. ...1...
. . '.'ell .,... ..., ... 8O-11~ r..,.
. . ..Ject..; A. Ace.p'..'. .tt. ..a1tftc8'Ionl; V - V.lld
1
1-"'.._...
...'1
...
10 U
10 U v
10 U .
-------
STATION ,.
'.tr. 1.1.2.2-,
Stltton 0... chloro 'o'roc.loro
"_or 5a.,lod .'''.n. ......
",/1 .../1,
-.-----
$V-064 07/22/87 I U NIl
$V -014 07/07/. I U I U
$V- 014 0)/)0/.. OIlY
SW-OU OS/22/" I U V I U V
5W-OU 06/27/" I U V I U V
SW-014 07/1"" OIlY
5W.064 01/11/" OIlY
SW.OU °'/20/" OIlY
5W.OU 10/0.'" DAY
SW.OU 11/0./.. DAY
SW-OU 12/01/" OIlY
SW-064 Ol/OS/IO DAY
5W-OU 02/02/10 DAY
Volatile
10l...n.
"./1
---- -- -----
"A
S U
I U "
I U "
. ~.~ .-
Surfaae Water
organia Sa.pling
(.Ioro
-.......
"./,
..
I U
I U "
. U "
VALUE QUAllfIER5: "R. Analyto not roportod U . Analy.ad but no' 'otoc'o'
J - Pro..nt ..10. 4.'.ctloft ".'t . . Pro..nt 1ft '...re.err ~1.".
DAIA VAllPArlOH QUAlfIER5: (No vollda.lon ~uall'lor Indlca.a. '0'0 ~O. no. boon ..11'0'''.)
I"'"
......".
../,
..
5 U
I U "
. U "
Results
St,rono
"'/'
--
..
5 U
I U "
. U "
'otol
."0""
"'/'
l1li
5 U
I U "
. U "
(
~.
. . No""" tt- ..0' -, I . 10".'" .010.0
N . ..tc" .,t'. ft.' I" 8O.11ft rl..,.
. - ..Ject.., A - Acc.,t..', ..,. ~y.'tf'c.'t.".&
-------
Volatile
STATION 103
Statton O.'e C"loro Ir- 'In, I
"""er 50.,lod _U..". ..t"ono C"'orldo
u./1 u.I' U8/'
-- -- --" ---- -..----
SW-IOJ 0'/"/" 10 U I' U 10 U
SW-IOJ OJ/n/.. 10 U , 10 U , 10 U ,
SW-IOJ 0'/"/" 0... ne' ,ea rocO hod
SW-IOJ 0'/15/" 10 U , 10 U , 10 U ,
SW-IOJ o,/n/.. 10 U , 10 U , 10 U ,
SW-IOJ 0./02/.. 10 U , 10 U , 10 U ,
SW-IOJ 0'/0'/" Oa'8 "01 "ot rocohod
SW-IOJ 10/OJ/" 10 U 10 U 10 U
SW-IOJ ../OJ/.. Dote not ,et rac.t"..
W-IOJ 12/0./.. Dote not "ot rocol....
SW-IOJ 01/../90 Dote not '0' roco "od
SW-IOJ 01/1'/90 0"1 "01 rat rac.lv."
SW-IOJ OJ/U/90 Dote no' ,at racelvad
. ~.,~ ...
Surface Water
organic sa.pling
Results
1.1-01- I.I-DI-
C"'oro """,,'ono Corloon ellioro ellioro
otll...o elllorl'" Acaton. Dh.UI... otllo.o otll..o
"1/1 "'/' ..1' ...,. ...1' .8/1
-- .-.--
ID U IU 10 U IU IU I U
10 U , I U V 10 U , IU V I U V I U V
10 U V 5 U V , JI " I U v I U V I U v
10 U , .. " 10 U , I U , IU v I U ,
10 U , I' " 10 U , I U V I U , IU ,
10 U 8. 10 U I U 5 U 5 U
. . Mo"ln. tl.. no' ... I . 10'I..to' .0'..0
" . '.tell ..1110 n.' In 1O-12Ga ron.o
. . 'oJoc'O'1 A - Aceo.'o"'o .Itll ~uollt'eo'lonal
VALUE QUALifIERS: NR - Anol,.o no' ropor'o' U . Anol"od "u' not ".oc.o'
J - Pr.'.Rt '.'0. ..'actloft '1.11 . . 'r.'.R' 1ft '...r.t.r, ~..ft'
DAIA VAIIDAIION QUAl'IERS: (No vall..'lon qu.'lfl.r Indlc...a d.'. ".a no' ....n v.'I..'.'.)
II - Vo",
.l
-------
STATION 103
lohl-I,2-
5""0" De'. Olc..lo.o I
"_0' 5...1041 eth.n. C..,...,....
",/1 "'/' .
SW- 'OJ 01/11/.. .. s U
SW-IOJ OJ/n,.. s U V S U V
SW-IOI OS/21/" D.'. ..0' ,., rec.'"e.
SW- ,OJ Of/IS/" s U V S U 'I
SV-IOJ 01/n/.. s U V S U V
SW-IOl 08/0'/" S U V 5 U 'I
SW-IOI 0'/0'/" o.to ..0' ,., r.cat",.d
SV-IOI 10/01/8. 5 U 5 U
SW-IOI II/OJ/" O. to ..0' ,., recetv.d
SV-IOJ .,/0./.. 00'. ..., ,., receev.d
SW-IOJ 01/1./10 D... ..., '0' rec.I....
SV-IOI 0,/.,/10 O. to ..0' ,., rec.'ved
SW-IOJ 01/"/10 OU' ..0' ,., recat.e"
. ,. .-
",
II-
Volatile
Surface Water
Organic sa.pling
Results
1,2-01- 1,1.1-1.1 Cerbon 1.- 1.'-01-
chloro c"'.r. ,.,.. '11..,1 ..c..,... ."'.r.
.th.n. ,.""....... .,...... cI,lorld. ac...,. -,...... .r.,....
",'1 ..." ..,'I "." .../t .../t .../t
--
su 10 U 1 U , 10 U 1 U 1 U
IU V 10 U 'I 1 U 'I 10 V 10 U V 1 U V . U V
5 U V 10 U V 5 U V , V 10 U V 1 U V 1 U V
IU 'I 10 U V 1 U 'I . V 10 U V 'U V . U 'I
5 U 'I 10 U V II U V 1 'I 10 U V 1 U V 1 U II
5 U 10 U 5 U 5 U 10 U II U S U
. . Holdh, tI- ..0' -, I - htl_'ocI ".tn
H . '.'C" .,It. "., I.. 8O-IIGS r...,.
. - AeJected. A - Acc.pt.~'. .It. .ye"ftcettonl;
'IALUf QUAL If If AS. "A - -...1". "0' '.'0.'.41 U - A...I,..4I ,,,, "0' d.'.ct.d
J . Pr...,,' ..10. ~.t.ctton 1..1' . - 'r....' fa '."ra'err ~,...
OAIA VAlloaltOM QUALfIEAS: (No vll'd."on ~y..tf'.r 'ndlc.... dl'. h.. "01 b..~ ~.,.~.t".)
-------
~.~ .-
8urrace Water
Volatile organic 8a.pling Results
8TATION 103
Ch-I,J- Otbr08O I.I.'-Irl
5,.,'on De'. Olc"loro Irlchlo':o cll1oro chlere
"_er 5...le' ,ro,.". .,...... _U'An8 .,...". I."..".
..,/1 .../1 .../1 .../1 "'/'
-.---- --.---- -- -_.__.--- --
SW-IOJ 01/11/88 5 U . U S U I U I U
5'1-101 01/21/81 I U \/ , J A I U V . U \/ . U A
5'1-101 05/11/81 De.e ..0' ,e' reeetve'
SW-IOJ 01/ tI/.. !I U \/ I U V S U V !I U V !I U V
5'1-101 07/11/81 I U Y I J A I U V I U V I U V
SW-IOl 01/02/.. I U \/ I J A S U V I U V . U V
5'1.101 0./07/81 Dete ..ot ,e' reeetv.'
5'1-101 10/01/11 !I U 5 U S U !I U S U
5'1-101 11/01/11 O.'a ''0' ,.t r.cetv..
5'1-101 11/0'/" Dete ..e' ,.. ree .tv..
SW-IOl 01/11/.0 0... "o1 ,.. r.c.tv..
$W-IOl 02/12/'0 O..a not ,at raee'v."
SW-IOl 01/12/.0 081. ..01 ,.. r.c.lv.'
In...-I. 1-
Olch'oro
,rop."e
.../1
II U
I U V
!I U V
I U ,
I U V
5 U
'-Me"'" -
,-.."..
'r_fe.. ..A. '''''''.._e
"'/' .../1 ..I'
I U 10 U 10 U
. V V 10 V V 10 V V
I U , 10 V \/ 10 V II
I V . 10 V , IOV .
IV V 10 V , 10 V V
5 V 10 U 10 U
\/AlU[ QUAll'I[AS: HA - 11....1,.. "0' r.por',. U - 11....1,... ...t ..ot ..tect..
~ . 'r...nt .a1ow ..tactlon I..tt I. Pr...ftt 1ft I."r...r, ~1.A'
DAIA VAllDAIION QUAl'I[AS, (Ho ...11...10" 4...II'I.r ,..'Ic.", .... h.. "o~ b.." v.II.......
. - Me"'". tt- ..0' _t « - htt_t" v.I...
" - ..tch .,I'e llet I.. BO-11Ga r...e
. - ,.J.C'.'I A. Acce,..'le .Itll ~...llflc.'lo"'1
V - v.lI.
-------
STATION 103
Stet ton 0.'.
Hu..or So..lod
$V.IOJ
$V.IOJ
SII-IOI
SII-IOJ
SII.IOJ
SII-IOI
SII-IOI
SII-IOJ
SII-IOI
SII-IOJ
- SII-IOI
SII-IOI
SII.IOI
-- . -- .---
01/11/88
01/21/"
OS/25/.'
01/15/.'
01/U/.'
08/02/.'
0./01/.'
10/01/..
11/01/.'
12/0./..
01/1./90
02/12/90
OJ/22/9O
t.tra
c"lero
e,tt.".
u,/I
..----
2 J
J J A
1,1,2,2.-
'o'nc"lero
0'''0''.
u./I .
---
0.'8 not ret rec.lved
, u
'U "
I J A
2 J "
2 J "
08.. not r.'
I J
D.'. not re'
Do" not r.'
DUo not ro'
Do" not ro'
Do" no' rot
5 U "
I U "
I U "
rlcelvl"
5 U
recetved
recelvld
recelvld
rlCe'vI"
rlcl''''ld
~:\ ...
Volatile
Surface water
organic .a.pling
Results
C"lor. IIlIrl 1.'.1
'oluln8 ......... ..."..". S'rr.". .,'...a
u./' u./' u./' u./I u./'
- --- ----- ----
I U I U I U I U . U
I U A I U A . U " , U " IU A
5 U " 'U v S U v S U " I U v
I U v I U V I U v I U " . U v
S U v I U V I U " I U " IU v
S U I U I U S U I U
VALUE QUALIfIERS: HR. ""ol,to not roportod U . A.ol,..d .ut ".t d.'.c'.d
J . 'ro.o"t ...10. do'octlon 11.lt I . Pr..on' I" 'o..r.'or, .10.'
D"'A "ALIDAIIOH QUAlfIERS: ("0 volldo.lon quollf'or Indlc..o. dO'O "0. not boo. valldo'.d.)
. - Helda". tI- "0' -t I - 10""'M velu.
M - lo'e" .,n. "., a.. 8O-IZOI n"..
A - .0Joe'.d; ". Aee.,'o.lo .1'" quallfle.'lo".;
..
..
-------
-------
.
..
APPENDIX B-2
SURFACE WATER SAMPUNG RESULTS
DISSOLVED METALS
SUFl~ACE WATE!> INTEFI1M FIEMEOIAl AC'110N PI.AN
::IQCi(V "cATS "u>."'"T. GOlDEN. COLOAAOO
eg&; ~Ir~ --.,n\.f.. apgenC.P91
-------
'., ~
surfaae .ater
Dissolved Metals sa.pling Results
903-PAD AND LIP SITB
St.tlon O.t. A lu...1 nuflt IIn'l-n.. Ar..ntc lorl- 'or..11I- C,..I- Calc 1- C..I- Cllr.l-
Hu.'.r 58-.lod (III). ..I... (511), 41... (II'). "I... (1a).41... (Ie), 418'. (Cd). 41... (c.). ...... (Ca), 418.. (Cr), 418a.
.../ I .../. .../. ../. ../. 81/' ../. ../. ../.
--.-.-- .------_u- '------ -....--.- .--
W-050 / / OR'
W-050 07/21/87 0.2 U NA Nil 0.21 NA ItA 141 IItII 0.0' U
511-050 06/17/" .282 .040 U .010 U .210 .005 U .005 U III .. .010 U
511-050 06/"/" In,..tllct.n' 58"'0 or Ol..olvod Mo..1t 1In..".. .0' ro"....'o".
511-050 04/17/" OR'
511-050 05/10/" OR'
511-050 06/211" -200 U V .0600 U II .0100 U II .100 U V .0050 U II .0050 U II 110 " IU , .0100 U ,
511-050 01/"/89 .120 II .0600 U , .0100 U , .1111 ' .0010 U , .0050 U , II' , IU , .0100 U ,
W-050 081 III" ORY
511-050 0"12/89 OR'
$11-050 10/04/" OR.
$11-050 11/0.'" OR'
$11-050 U/Ol/89 OR'
$11-050 01/°5/.0 ORY
$11-050 02/02/90 OR'
511-050 0.' 17/.0 OR'
511-0S1 0"21/87 0.2 U Nil Nil 0.11 NIl ItA 101 NIl 0.01 U
W-051 06/21/88 ORY
$11-051 04/1718. OR'
511-051 05/10/" ORY
511-051 0"21'" .200 U , .0600 U " .0100 U , .100 U , .0050 U , .0050 U " ".10 " IU , .0100 U ,
W-051 01 I 18/" ORY
511-051 081 III" OR'
W-OII 0'/12/" ORY
$11-051 10/04/" DA'
511-051 11/0)/" ORY
511-051 12/°1/" ORr
511-051 01/05/.0 DAY
511-051 02/02/90 DAY
511-052 07/21/87 0.2 U Nil Nil 0.2 U Nil ItA 110 .. 0.01 U
511.011 06/21/88 .89' .040 U .010 U .20 U .005 U .005 U .... .. .010 U
511-052 04/17/8. DAY
511-051 01/10/" ORY
511-052 06/°'1" ORY
'"lUI QUIILlfl11l5: Nil. IIn,I,lo "0' ro,or'." U . IIn,I,.... II.., "0' ".'oc'o"
~ . 'ro,.n' "o'ow "oloe'lon '1.11 1 . 'ro"n' I. ',"'ra'or, "Ia.'
0"'" '''LIOA'ION QI'''lfIIA5: (No vol''''llon "..,'I'I.r In"'c,'" ..", ~" no' b"n .,II..a,....)
I
. . ......Inl .1.. "., ... 1 . 1,.1...... ..1...
It . .,..~ "", not 'n 8O-12err. ".'0
R . .'J'c',", II. IIec,p""" .1.11 "..,.I'I.,'Ion" ,. ,.'1"
of
-------
.
...
. ,
surface water
Dissolved Metals sa.pliDCJ Results
'O)-PAD MID LIP SITB
S,.tio" 00'0 Cobolt Copp.r Iron l.oll U'''I- Mo,nool- Mon,o..... Morellr)' Mo"W..-
H'-or 50...I.d (Col. dl... (ell), III... (10). dioo. ("). II".. (U). ..... (Ntl. 11"0. (MIl), d"" (Nt). dl... (Mo). II"..
89/' "/' "/' "/' "/' "/' "/' "/' "/'
..-----.- -..---- ----~- -. -- ----
$\/-050 / / 011'
$\/-050 01/21/81 0.05 U O.ou U 0.1 u NIl HA '.0 0.4'11 HA 0.04 u
$V-OSO 08/21/" .010 U .021' .114 .001 U NIl ..U .00" .0002 U NIl
$V-OSO 08/21/" I.o..ffle I...' 5000p'. or Oluolv.d Moto II A...I)'." ..0' r.,,,.,'.d.
$V-OSO 04/11/.. 011'
511-050 05/10/" 011'
511-050 00/'11/" .0500 U V .0'150 U V .100 U A .0010 U I .100 U A '.41 V .148 V .0002 U V .100 U A
$V. 050 01/11/.. .0500 U V .0210 U A .552 A .0010 U " .100 U V '.11 " .... ., .0001 ., .100 U V
511-050 08/11/" 01'
5W-050 0'/1'1/" 0'"
5W.050 10/04/89 OA'
5w.050 II/OJ/89 011'
511-050 I'I/OI/at 01'
5W-050 01/05/'0 OA'
511-050 02/02/'0 OA'
$V-050 0)/11/'0 OA'
511-051 011'11/81 0.05 U O.OU U 0.1 U NIl HI 1.' 0.011 U HI 0.04 U
$\/-051 OfJ/ZJ/.. 01'
$V-051 04/11/" 01'
5W-051 05/10/.. 01'
5W-OSI 00/21/" .0500 U V .0250 U V .100 U " .0010 U . .100 U " 1.14 V .0110 U . .OOOZ U V .100 U "
511-051 01/11/.. 01'
$\/- 051 08/11/.. 011'
$V-051 0'/12/" OA'
511-051 10/04/" 01'
$V-OSI II/OJ/" 01'
$V-OSI 12/01/.. 0'"
5W-OSI 01/05/'0 OA'
5w-051 02/°'1/'0 DAY
511-052 01121/81 0.05 U 0.025 U 0.1 U HI HI n.l 0.111 NIl 0.04 U
5'1-05'1 08/21/11 .050 U _024 .51 .005 U HI !J.I .0'" .0002 U HI
$V-OS'l 04/11/.. DAY
$V-OS2 05"0/" DAY
$V-OSI 01/0'/" OIlY
VALU( QUALlflfR5: HA - An.I)". '0' ropo,'.d U - A..ol)',od ..., ..0' '.'.e'"
J - Pro...' '.Iow '.'.e"o.. I'." . - 'r.....' I. I...r.'.r, .,..,
DA'A VALIDA'ION QUALflfA5: (No v.II'.'lo.. q..oll'I.. ,..die.'., do', ho. "0' b.... v.I'd.,...)
. . Mo'''., 11- ..0' -, I . (011-'.. v.,,,.
M . '.'eh .,1'0 ..., I.. 80-'201 r..,.
-------
...,
8urface Water
Dissolved Ketala Sa.plinCJ Results
,03-PAD AND LIP 8ITB
5'.'Ion D.'. Hlc..1 ,.....1"'; S.'.n".. SlIv.r SMI- Stront 1- '...111- 'h. V.....I-
H-.r 5..,1.01 (HI). 011... (II ). ..... (So). "I... (Ae). .1... (lie). ..... (Sr). .1... (II), ..... (S..), ..... (V). .....
..,,11 "/' ..11 ../1 ../1 .../1 ../1 ../1 ../1
-. >--.. .- -- --- ---- .----
$W-050 / / DAY
$V-OSO 0'/21/11 0.04 U HA HA 0.01 U '.$ 0.41 NA HA 0.0$ U
511.050 0'/21/" .040 U $.21 .005 U .010 U 8.U .J8' .10 U .. .010 U
511.050 0'/'11/" 1.....'ft
-------
.
Surface Water
Dissolved Metals sa.pling Results
'03-PAD AND LIP 81TB
St.tton 0.'.
Muabor $o~lod
$\1-050
$\1-050
511-050
511.050
511-050
511.050
$\1-050
$\1-050
$\1.050
511.050
511-050
511-050
511-050
511-050
511-050
511-050
511-051
$\1.051
511-051
511-051
511.051
511-051
511-051
'"-051
'"-051
'"-051
511-051
'"-051
511-051
511.05Z
511-052
511-052
5\1-052
SW-052
- ..-----
/ /
07/ZI/.'
"/21/11
"/21/11
04/11/"
05/10/"
01/27 /"
01/11/"
0./11/.'
0./12/..
10/04/..
II/OJ/..
12/01/..
01/05/.0
OZ/02/1O
OJ/I1/1O
07/ZI/81
01/21/..
04/11/..
05/10/"
Ol/Z1/"
01/1./..
0./11/..
0'/12/"
10/04/"
II/OJ/..
12/01/..
01/05/'0
02/02/10
01/21/81
01/21/11
04/11/"
05/10/"
06/0'/81
Zinc
er..). dl...
../1
011'
0.02 U
.0JlI
I..outflcl...t
011'
011'
.0200 U V
.0200 U A
OIlY
OIlY
OIlY
DA'
ORY
ORY
ORY
OIlY
5.-p1. .r Dlooolyo. Mo.olo A..ol,olo ...t r.~uoot.d.
0.02 U
OIlY
011'
OIlY
.0200 U V
ORY
OIlY
ORY
ORY
OIlY
OR'
OIlY
ORY
O.OZ U
.0JI5
ORY
OIlY
OR'
VAIUI QUALlfIIR': HR. A..ol,.. ..0' ropor'o. U . Anol,.od bu. ..0' ..toct..
J . 'r...nt be'ow d.'.ct'oR .,... . . 'r...n' tft '.~.r.'.r, .1...
OAIA VAIIOAIION QUAlfIIA5: IMo .olldo.lon quollflor Indlco,o, do.o hoo "0' bo... yolldo....)
. - Moldl... tt- "0' -. 1 - lott_to. y.lu.
M . ..tch 0,1'. ..0' 10 80-1101 ro..,.
. . .oJoc.o.; A. Ace.p.o". .It' ~uo'I'leo.lo..o; V. Vo'i.
-------
...\
Dissolved
8urfaae .ater
Metala 8a.plinCj
Reaulta
'03-PAD AND LIP 8ITB
Stet ton Dete A'umtnU8 II..'I_"r IIr.."lc ..,1- lerrlll- C..I- C8lcl- C..I- C.,_I-
"_.r S..,I.d (III). dll.. (n), dl... (II.., dl... (I.., dl... CI.), dl... (Cd), d"" C(8), dl... (C.., dl... CCr), d''',
../1 ../1 , ..11 ../1 ../1 ../1 ../1 ../1 ../1
n - --- -_u_-~- ---------- ------ -- ----
SW.052 07/07/89 OIlY
SW-052 08/81/" OIlY
SW-051 0'/28/" OIlY
SW-051 10/0./" OIlY
SW-051 II/OJ,,, OIlY
SW-051 12/01'" OIlY
SW-051 01/05/90 DIIY
$W-052 02/01/'0 OIlY
SW-051 01/""0 OIlY
5\1-055 0'/21/87 0.1 U "II "" 0." "" l1li 12. "II 0.01 U
SW.055 07/11"7 1".u"lcl.n' 5_1. or DI..olv.d Mo,.I. IIn.lr." ..., r84u,"'..
SW-055 OI/U'88 .796 .0.0 U .010 U ..11 .001 U .001 U 1)1 "" .010 U
SW-055 0'/"/11 .100 U V .0100 U II .0100 U V .11) V .0010 U " .0050 U V ".70 V IU V .0100 U II
SW-055 01/25'" Do" no' r" rec.tved
SW - OIS 01/18'8' .200 U V .0100 U " .0100 U " .In V .0010 U " .0010 U " 10. " IU V .0100 U V
SW.055 01/18/.. .200 U " .0.00 U V .0100 U V ..11 V .0010 U V .0010 U V 118 V IU V .0100 U V
sw-055 08/11'" .100 U " .0100 U V .0100 U II .101 V .0010 U V .0010 U II III V IU , .0100 U ,
SW-051 0'/20/" .200 U II .0100 U V .0100 U V .... V .0010 U II .0010 U " US " IU II .0100 U II
SW-051 10' ",.. .0Joo U V .100 U " .0020 U V .111 V .0010 U II .0040 U " .., V .0010 U V .0100 U "
SW-055 11/0'/" .100 U .0.00 U .0100 U .111 .0010 U .0050 U IU IU .0100 U
SW-055 U/Ol,81 0.,. no' ,., recetv8d
SW-055 01/1"90 D.,. no' ,., rec.lv848
SW-055 02'U,'0 D." no' r" received
$W.01S 01/11"0 D.,. no' ,., receive"
SW-057 07/21/81 0.2 U "" "" 0.' "" .. "' l1li 0.01 U
SW-017 06/11/88 DIIY
SW -057 0""'" DIIY
SW.051 05/10'" DIIY
SW.057 0"0"" OilY
SW.OS7 01/01'" OIlY
SW.051 08'11'" DIIY
SW.051 0'/11/81 DIIY
SW-051 10/04'81 DIIY
SW.051 11 /01'81 DIIY
VAIU( QUAllfl(AS: Nil - An.lrt. no' r.port.d U - An.lr..d bU' "0' ..,.c,..
J - 'r...n' '.Iow ..'.c'lon 11.1' . - P,....., I.. I...,.,.r, .I...t
OAI" VAllDAIION QUAlfl(IIS, (No v.lld.tlon qu.II.I., Indlc.,.. d.t. h.. "o~ b..n v.lld.t...)
. . 1101.... 11- no' -, 1 - 1.11_'" v.""
" - '.'c' .,1'. n.' I.. 10.1101 r....
II - II.J.ct..; ,,- Acc.pt..I. .1" ~u.llflc.'lon.; V - v.l.d
-------
.
.
8urface .ater
Dissolve4 Metals 8a.pling Result.
,03-PAD AND LIP 81TB
Statton Oa'e Cobolt Co"or Iroft l... l"ha- "'1"00 a- Mo"lo...O. MercMrr Mo,,-.-
II_or So...I.d (Co), dl... (b). .ho. (fe), .1... C"). .1... (U), .1... (MI). .a... C...). ."0. CHI). .1... (Mo). .....
"/' "/' ../1 "/' ../1 "/' "/' .." ../1
..-- - --.-- ---- --.--- ---- ----- .._- --
W-O!l2 01/01/.9 DAY
W-O!l2 08/1 1/11 DAY
W-O!l2 01/2./.1 DAY
5W-O!l2 10/04/.1 DAY
5W-O!l2 11/01/.. DAY
W-O!l2 12/01/.9 DAY
5W-O!l2 Ol/O!l/IO DAY
W-052 02/02/10 DAY
5W-052 01/11/10 DAY
5W-055 01/21/81 0.05 U O.OU U 0-1 U ... .." 11.7 0.022 II" 0.04 U
W-05!1 0,/21/., l"o..Ulel."' 5....10 or Ohoolvo. Mo'olo A... 1"0 .. ut r......oto..
SW-O!l!l 0&/22/88 .050 U .025 U 1.0& .001 U HA 21.J -24 .0002 U H"
SW-O!l!l 04/11/89 .0500 U Y -0250 U A .128 A .00!lO U A .0115 A 20 ' .Jr4 ' .0001 U A .0201
SW-05!1 O!l/25/.' DolO no' 'A' recetve"
SW-O!l!l 06/28/8. .0500 U , .0250 U A .100 U A .0050 U , .100 U A 18.10 ' .0740 ' .0002 U , .100 U A
5W-05!1 01/18/.. .0Soo U , .OUO U A .100 U " .0050 U " .155 ¥ 11.80 It .470 It .0001 U ¥ .100 U It
SW-05!1 08/ "/8' .0500 U , .OZSO U " .100 U " .00JD U " .11' " II.. It .HI It .0001 U It .100 U It
SW-055 09/20/.. .0500 U It .0250 U ¥ .100 U " .0050 U " .111 " 28.. It .111 " .0001 ¥ .100 U "
SW-05!1 10/"/8' .0200 U , .0200 U " .05!14 " . 0020 U " .115 " n.2O ' .145 ' .0001 U " .100 U "
SW-05!1 11/0./89 .0500 U .OUO U .100 U .0050 U . "I 25.10 .110 .0001 U ,100 U
W-O!l!l 12/01/.. Ooto no' 'A' receive"
SW-O!l!l 01/1./10 Do,o no' ..A' recet"..
5W-055 02/21/10 Dote no' 'a' received
W-055 OJ/I5/1O Date "0' "0' rac.tveet
5W-051 0,/21/.' 0.05 U 0.025 U 0.1 U "" "" 21.' 0..1 "" 0.04 U
W-O!l1 Ol/U/.. DAY
N-O!l1 04/11/.' DAY
SW O!l1 O!l/IO/89 DAY
SW.051 06/0./8. DAY
SW-O!l1 07/01/89 DAY
N-OS1 08/11/.' DAY
SII-051 0./ "/.' DAY
SII-051 10/04/.. DAY
SW-O!l1 11/0)/89 DAY
'AlUt QUAllfltAS: HA - A"ol"o .0' roporto. U . A"ol,.o. b.., ..0' .otoe'o.
J . '.0"'" .010. .oteetlon II.." . . 'r.oont ,.. ""rotor, .10..'
. DAIA VA'IOAIION QUAl'I(RS: tHo y.'fdetton qu."ff.r 'ndlca'.. data h.. no' ~.." va"..'...)
. . "'1.1"1 tl.. no' ..., I . Iota...... vol..o
.. . h'eh 0'''. "., I.. 80- 12011. ro"l.
-------
'.,
Surface Water
Dissolve4 Metala sa.pling Resulte
,03-PAD AND LIP SITB
Stet ton De'. Hld.1 Po'''' I... hl.nl- Stl...r 50.1- SIron"U8 ,,,.111- ftn V....'-
H_b.r 5..,1.4 (HII. 41... lie ). .,... (h). 41... C".). .1... (No). 41... (SrI. .1... ('il). .,... (Sn). .10.. (V ). ..h..
""1/1 ../1 .g/I ../1 ../1 ../1 ../1 ../1 ../1
.. __d .--. - .----- -..--.- -----
SV.OSI 07/07/89 OIlY
sv-052 08/11/.' OIlY
SV-OSI 0./18/.. OIlY
SV-OSI 10/04/8' OIlY
SV-OSI II/OJ/89 OIlY
SV.OSI 12/01/8' ORY
SV-OSI 01/05/'0 OIlY
SV. 052 02/02/10 DAY
SV-052 OJ/I7/1O OIlY
SV.OS5 01/11/87 0.04 U HA HA 0.01 U JS.2 0.7J NIl Nil 0.05 U
SV-OS5 07/21/.7 In...'' I. Ion' 50...1. or 01..01...4 ...Ulo "n.I,. to .., r.,....'.d.
SV-OSS 01/12/.. .040 U 5 U .005 U .010 U 11.' .918 .010 U HII .050 U
SV-OSS 04/17/.. .0400 U " 5U " .0050 U " .0100 U " 4"10 " IU " .0100 U II .100 U V .0100 U "
511-0SS OS/25/8. 0.'. not rat racelved
SV-OSS 01/2./81 .0400 U " 5U " .0050 U A .0100 U " )4.20 " IU " .0100 U " .100 U " .0500 U V
SV - OSS 07/1./81 .0400 U , au " .0050 U II .0100 U II ".10 V IU , .0100 U II .100 U , .0IlOO U ,
511.055 08/1./.. .0400 U " 5U " .0050 U " .0100 U " 55.40 " IU , .100 U II .100 U , .0IlOO U II
SV.OS5 0'/20/8' .0400 U II 5U " .0050 U II .0100 U " ".50 " IU II .0100 U " .100 U " .0IlOO U "
SV.OS5 10/19/8. .0100 U A I.U " .0010 U " .0100 U II ".10 ' .7'" .0010 U V IU " .0100 U V
511-DSS 11/0./81 .0100 U 5U .0050 U .0100 U ".10 IU .0100 U .100 U .0500 U
511-0SS 12/07/.. Dou "01 ,.. race' vad
SII.OSS 01/11/.0 0.'. no' ,., r..."'..
511.055 Ol/U/IO Dou no' ,., recet".'
511-0SS OJ/I5/.0 0.'. no' ,., rec.t".d
511.057 07/11/81 0.01 U HA HA 0.01 U 20.1 0.7' NIl HI 0.05 U
$W-D57 O8/U/.. 011'
SV-057 04/17/81 OIlY
511.057 05/10/81 DAY
SII-D57 01/0./81 DAY
511-057 D7/01/8I OIlY
511.057 08/11/81 DAY
511.057 0./11/.' DAY
5V.OS7 10/04/81 DAY
511.057 11/01/81 DAY
""lUf QU"llflfAS: NIl. "n.I". no' r.por'.. U . "n..,..4 b.., no' ..,..,...
J . 'r...n, b.l~ ..,..,Ion II-I' . . 'r....' I. I.bor.'.r, bl..,
OAIA ""lIOAIION QU"l'lfA5: (Ho ..114.'lon ,...II'I.r In41..'.. 4.,. ".. no' b..n ...11..'...)
. - ...1.1., 'I. no' ., I . In'.,... ...1...
" . '.'.11 .,1'. n.' In eo-11ft r..,.
I . ..J..'..; ". "....,.bl. .1'" ,...llf'..'lon.; ". '.11.
.
-------
,.
'.,
Surface Water
Dissolve4 Ketals Sa.pling Results
'03-PAD AND LIP SITB
ZInc
U"), "hi.
../1
Slit Ion D...
lI_er 58..,I.d
--..---
N-OU 01/01/"
N-On 08/11/1.
SW-OU 0'/28/"
SW-OU 10/04/"
SW-OU 11/01/8.
SW-OU Il/OI/8.
SW-OU OI/OS/tO
SW-OSZ oz/oi/tO
SW-OU 01/I7/tO
SW-OSS 07/21/81
SW-OSS 07/21/81
SW-OSS 06/U/..
SW-OSS 04/U/8.
SW-OSS OS/25/8.
SW-OSS 06/Z8/8.
SW-OSS 07/11/8.
SW-OSS 08/11/8.
SW-OSS 0./20/8.
SW-OSS 10/../8.
SW-OSS 11/0./8.
SII-OSS 12/01/8.
SII-OS5 OI/II/tO
Sw-oSS 02/U/tO
SW-OSS OJ/IS/tO
SW-OS1 07/21/87
SW-057 M/U/..
5W-OS7 04/11/8.
5W-OSP OS/10/8.
SW-051 01/0./8.
SW-OS1 01/01/8.
5W-OS1 08/11/8.
SW-OS1 0'/11/8'
SW-OS1 10/04/"
SW-OS1 II/OJ/8.
... --_.. --
OIlY
OIlY
011'
OIlY
OIlY
OIlY
OIlY
OIlY
OIlY
0. ..
In.uttlct.nt 5...,. or Ot"OIV8d He,.,. An,I.,I" fte' r.......,.tI.
.5)6
1.21
y
Oa'e not ret recetved
.S51
.no
....
.ltl
.8"
1..0
0.,. "0' 1'.'
0.,. "., ,.,
Oa'. "., ,.,
0... "0' ,..
,
"
,
"
"
raceivi.
rec.ln'
rae.lwad
racat".ct
0.02 U
011'
OIlY
OIlY
011'
011'
OA'
OA'
DA'
DAY
. . ......", tt- .0' -, ( . htt-.... ...Iu.
M . '.tch .~1'. ".t I" 1O-llOa r..,.
. . ..J.ctld& A. Accep"." with ~w.'t"C"t'R'; ¥ - V....
'''Lue QU"LlfleAS, IIA. "".11". .0' r.~or'.d U . "".ll'o.d but .0' ".'.ct.'
J - 'r..,,., ~.'o. ..,.ctton 1'.1' . - 'r...nt 1ft '...r.'.r, .'IA.
-------
surface .ater
Dis801ve4 Hetala S..pliDCj .esults
'03-PAD MID LIP SITB
Stetton 0.'8 A'UMlnuM A..tl-.... Ar..nte I..t- ......111- C._I- Celcl- Ceet- C"r_I-
"_.. 5e..le" (AI). "I... (U), cI"e. (A'). .h. - (b), .1... (I.), .1... (Ut. ..... (e.), ."e. (el), .1... (er), ."1.
"'9/1 ../1 ../1 ../1 ../1 .,/1 ../1 ../1 ../1
- - u-------- - ------- -- ---- -- --
SW-OIl1 12/01/89 DAY
N-OIl1 01/05/'0 01'
N-051 02/02/'0 DA'
N-051 OJ/I1/'0 DA'
5W-058 01/21/81 0.2 U l1li HII 0.2 U NIl "II III HII 0.01 U
SW-OIII 06/21/18 .20 U .040 U .010 U .nl .0011 U .0011 U 101 .. .010 U
N-Oil. 04/11/89 01.
N-058 05/10/1' DAY
SW-05' 06/2./8. .200 U A .0600 U , .0100 U , .204 V .0050 U A .0050 U V 101 V .100 U V .0100 U V
5W-05. 01/14/8. DAY
SW-05' 08/11/8. DA.
SW-05' 0'/20/" DA'
SW-OIl8 10/04/" DA'
N-05' 11/20/" 01'
N.051 12/01'" DA'
SW-051 01/05/.0 01'
5W-058 02/02/'0 DA'
SW-OH 06/22/88 .669 .040 U .010 U .2511 .001 U .005 U 110 NIl .010 U
SWoon OJ/Jo/" DAY
N-on 05/11'" DA'
SW-011 06/21/89 .200 U A .0600 U A .0100 U II .200 U V .0050 U V .0050 U V "I V .100 U V .0100 U A
N-on 01/11/" Oil.
N-on 0./16/89 .200 U A .0600 U , .0100 U A .200 U V .0050 U , .0050 U A n.. v IU V .0100 U V
SW-011 0./20/8. OA'
swoon 10/04/" OA.
swoon 11/09/" OA'
swoon 12/01/.. OAY
SW- on 01/05/.0 OA'
SWoon 02/02/.0 OA'
SWoon OJ/16"0 De" not ,et recetved
VALU( QUALifiERS: HII. A..el,te ..ot re.orted U . "".I,.e" byt ..ot det.ct..
~ - Pr...ft' ..10. ....ctton 1..lt . . Pr....' t. I...r.'.rr .,...
OAIA 'ALIOAIIOH QUALfIIAS: ("0 vell"etlo.. ~y.II'I.r I.."lcete. ...te h.. ..ot be... wIII..et...)
.
. . 1181..1.. tI- ..ot _t I . IIII-t... ...Ive
It . htc" ..1" ..et I.. 80-12. re.,.
I . ReJect.", A. Acee,t."le .It.. ~vellflcetlo"'1 V. velld
t-
-------
t
,
8urface ..ter
Dissolved Hetals ...pliDCJ aesults
903-PAD 1UfD LIP 81TS
Station 0... Cobo" Copp.r Iron l.o' lltlll- ...,....1- .......,.... Mercur, ...,,wo..-
"_or 50..I.d (Co), dl... (C..), .1... (f.), dl... ('.., .1... (Lt), .1... ("I., ."0. (...., .. u. ("I), ..... (...., "u.
""1/1 "/' "'/' ..I' ../1 .'/' "/' "/' ../1
-- ..--. ------ -.---- -~-- -...---- ---- --
$W-OSI 12/01/" DAY
$W-OSI OI/os/tO DAY
$V.OSI 02/01/tO DAY
$W.OSI OJ/11/"0 DA'
5W.OS8 0,/11/" O.OS U 0.025 U 0.1 U "- . !J.' o.on . 0.04 U
$W-058 M/ll/" .050 U .025 U -.10 U .005 U . 1'.tO ,OIl' .0002 U .
$W-OS' 04/11/.. l1li,
$W.OSI OS/IO/.. IIIIY
$V.OSI 06/21/.. .OSOO U V .02S0 U A .100 U A .0050 U A .100 U V II.SO V .0150 U V .0001 U V .100 U V
$V.OS8 01/14/1. DAY
5W-OS8 08/11/.. DAY
$W-OSI 01/20/" DA'
$W.051 10/04/1. DAY
$V.OSI II 120/" DA'
$V.OSI Il/OI/.. DA'
$V-OS' Ol/OS/'O DAY
$W-051 01/01/.0 DA'
5W-011 06/22/88 .050 U .025 U I. 48 .01" "- 22.1 1.14 .0001 U .
$W-on Ol/JO/.. l1li,
$V-OIl OS/II/I. IIIIY
5W-Oll H/211" .OSOO U V .0250 U V .100 U A .0050 U II .100 U V n.tO V .OUI V .oool-U V .100 U V
$W-Oll 01/11/" DAY
$V-OIl 01/11/1. .0500 U V .0150 U A .100 U A .00.10 U A .100 U V !J.l0 V .158 V .0001 V .100 U V
$V-OIl 01/20/.. DAY
$W-011 10/04/.. DA'
$W-Oll II 1°9/.. DA'
$V-OIl 12/01/" DA'
$W-Oll 01/05/.0 DA'
$V-OIl 02/011"0 DA'
$V-011 01/1"'0 oete not yet recetved
VAlUE QUAlifiERS: "R - Anol,.. no' r.por'.' U - An.I,... ..., "0' ..,..,..
J . Pr...nt b.'OM _.'ectloft .I.lt . - 'r....' t. '...r.t.r. .....
DAIA VAllDAIION QUAlfIEAS: ("0 v.lld..lon quo'I'.or 'ndleo'.. do.o "00 "0' b..n vo'ld.'.'..
. - Mo"'.., ,... .., .., I - I."..,.. v.'u.
M - '.'ell .",. n.' ,.. 10-1201 r.....
-------
surface Water
Dissolved Metals saapliDCJ Results
'03-PAD AND LIP SITB
St.tton De'e Hld.1 'ot...I- 5.I.nl- Slhor ,0<1,- 5trontt- ...111- Itn V.n.'I-
H.-.r 50."., (HI), dl... (II ). ,.... (50). dl... CA,). ,.... CH.). tit... C5r). tit... cn). ,.... CSa). ,.... C" ). ,....
"'9/1 "/' .../1 "/' "/' .../1 "/' "/' "/'
._.--- -.---- ... ------- ------- ----- -..---- -- ---
$V-OS1 12/01/81 ORY
SV.OS1 01/05/'0 ORf
SV-OS1 02/02/10 ORf
$V.OS1 OJ/I1/.0 ORf
5\1.058 07/21/87 0.04 U HI HI 0.01 U II.I 0.111 NIl NIl 0.011 U
SV - 058 06/2J/.. .040 U 5 U .005 U .010 U 11.10 .111 .10 U .. .010 U
SV.051 04/11/11 ORf
511.058 05/10/8' ORf
511.058 06/28/11 .0400 U V 5U R .0050 U A .0100 U V 1.21 V .418 " .0100 U A .100 U V .0500 U V
SV.OS8 01/14/8' ORf
SV.OS8 08/11/11 ORf
SV.058 0./20/11 ORf
$V-058 10/04/11 ORf
$V-OSI 11/20/89 ORf
$W-OSI 12/01/89 ORf
SV-OS8 01/05/.0 ORf
511-058 02/02/.0 ORf
511.017 06/22/88 .040 U 5 U .005 U .010 U 54.1 .sn .010 U .. .050 U
SV-017 OJ/1O/89 ORf
511-011 05/11/11 ORY
SV.011 01/27/11 .0400 U V IiU " .OU4 V .0100 U " 41.40 V .lill " .0100 U " .100 U " .0100 U V
511 -011 01/'8/89 ORf
SV-011 08/11/" .0400 U V '.04 V .0500 U V .0100 U " 2J.60 " IU " .0100 U I .100 U v .0500 U I
511-011 01/20/" ORf
5\1.011 10/04/11 Dlf
511..011 11/0'/" ORf
SV.011 12/01/" ORf
511.011 01/05/.0 ORf
511-011 02/02/.0 ORf
5\1.071 OJ/ II/tO 0.'. not ret received
VALUE QUALifiERS: HI - An.l,to not roport... U - An.I,.... 'ut not ,.t.c'.'
J. 're..ftt ~.1o. ~.t.ctloft 11.lt . . 'r...At ,. ....r.,.r, ....~
OAIA VAliDATION QUAlfIEI5: (Ho yoll'ollon qu.ITf'or Ind'c.t.. d... n.. nat .... y.'I'.to'.)
. - Noltlt.. 11- ..ot _t I - htl_t.. ...1..0
H - '.tc. .p.to not I.. 1O-llGa ro.,.
I - ..Joct.', A - Acc.p,..lo wI'. ~u.I'flc.'lon'l V - '1.11'
-------
'G)-PAD AND LIP SITB
Statton O.te Itn'
N-er S...I.d ."'). dl...
../1
-_.._-- .---.-..-
$W-057 12/01'" OA'
$W-OS7 01/05'" 011'
$W - 057 02/02"0 DA'
$W-OS7 OJ/I7,.O OA'
$W-OS8 07/21'.7 0_02 U
$W-OS. 06/U," -0256
$W-OSI 06/17'.' OA'
$W-OSI 05/10'.' 011'
SW-OS. 06/2.'.' _020' A
SW-OS8 07/1.'.' DAY
SW-OS8 08/11'.' OA'
$W-OS8 0'/20'.' OA'
SW-OS8 10/0.'.' OA'
SW-OS8 11/20'.' OA'
$W-OS8 12/01/.. OA'
SW-OS8 01/05"0 OA'
SW-OS8 02/02"0 OA'
SW 011 06/22/88 .0671
N-017 OJ/IO/.. OA'
N-On 05/11/8. 011'
N-On 06/27'.' .0286 A
SW-017 07/18'.' DA'
SW-017 08/11/.' .015. A
swoon 0"20/.' DR'
swoon 1°/0./.. OA'
swoon 111°".' OA'
swoon 12/01'8' OA'
N-on 01/05/.0 DR'
N-07 7 02'02"0 OA'
swoon OJ/II,.O D.'. not r.' rae.tved
Dissolved
Surfaae Water
Metals sa.pllng
VAlU[ QUAllfl[AS, "A - Anolroo noO roporO.' U - Anolr..4 ~uO noO ....c...
J - Pr.'on. bol.. 'o.oc.lon II.'. 1 - 'rooo.. In loboro.or, 'Ion'
OAIA VAllOAIION QUAlfl[AS: ("0 vol"otton quollflor In4'cot., dot. ~o, no. boo. voll'.....)
Result.
. - He141ftl tt.. Rot ..t I - 18'1..,.. value
M - 'otc~ 0"'0 n.. I. 80.1201 ro.,o
A - AoJ.c.o'; A - Accop,oblo .It. quollflcotton,; V - Volt.
-------
surface Water
Dissolved Metals
Sa.pling Results
STATION 53
St.,'on Vet. "Iu.'nUill Antl_nr Ar..ntc ..rl-- lerrlll- C...I- C.'cl- C..I- Cllr_l-
Nuu.r 50....d CAli. dl... (nl. 'ho. (Aol. d I... C'ol. ..... C'o). '''0. (U). ..... CCo). ..... (Co). '''0. CCr). '''0.
"'9/1 "/' , ../1 .." .." "/' .." .." .."
_0- . ------ ------- ---- ------ ---.-.-
;
sw.on 01/21'87 0.2 U HR HR 0.1 U HI NIl 80.0 HI 0.01 U
N' OSJ 06/1J/88 .141 .040 U .010 U .UI .001 U .001 U ..I ... .010 U
5W.05' 06/1J/88 InouUlclont 5...... or Ol..oh,od Mot... Anolro" no' ro"uooto'.
SW-05' 04/05/" .200 U .0600 U .0100 U .100 U .0050 U .0050 U 88.10 IU .0100 U
N.05. 01/1J/8. .200 U V .0800 U A .0100 U A .200 U V .0010 U V .0010 U . 104 A IU V .0100 U A
swoon 06/24/8. .200 U A .0800 U V .0100 U A .200 U V .0010 U " .0050 U V ... V .100 U V .0100 U V
5W-0!U 011"'81 DAY
sw-051 08/11/8. .200 U A .0600 U V .0100 U A .228 V .0050 U V .0050 U A 140 V IU V .0100 U V
5W-051 0'/20/" .200 U II .IU A .0100 U V .10' V .0010 U A - 0010 U V 117 " IU II .0100 U A
SW.051 10/1118. .200 U A .0600 U II .0100 U II .100 U V .0010 U II .0010 U II U, II 1.10 U II .0100 U V
SW.05' 11/011" O.t. not Jet r8C8 t "ed
SW-051 82/11/8. oete not ro' rocoh..
N.OSJ 0"11/10 0.'. not ,et race' v...
SW-OSJ OI/U/tO Dot. nol ,ot rocol VI'
VALUE QUALifiERS, HR - Anolrt. not roport.. U - An.lr..d but not 'otocto'
J - Prooont .olow doto.tlon 1181' I - "000.' I. 'o...otor, .'0..
DAIA VALIDAIION QUAL'lfAS: C"o .olldotlon "..oll'lor I"dlc.t.. d... ~.. no, ...n ..II.oto..)
. - ......., tI- not _t I - l.tI_to' """0
H - ht.1I .,1" not In 10-111170 ro.,o
. - ReJect.'; A - Accept..'. -I'. 4u.""C.'tOft8.
V - Volld
-------
.
.
Dissolved
Surfaae Water
Metals sa.plinCJ
Results
STATION 53
Station Oat. Cob. It Coppor Iron Lo.. L ,,"'- "',n..'" ....,...... Mercurr Mo',Wo,,-
II-.r Sa., 104 (Col. oil... (C..). ..... (hI. 081... (,,,,. .,... (LI). ..... (...,. .,... ("'). .,... (lit). ..... (Mo). .h..
.../1 "/' ../1 ../1 ../1 ../1 ../1 ../1 ../1
--..-.- . - -- -..._- _._~.- -..----- ---- -._- ---
$V-O~) 0,/21/.' 0.05 u 0.02t U 0.1 U NIl III 26.4 0.087 NIl 0.04 U
$V-on M/n/.. .050 U .0274 .2) .005 U NIl n.1 . lOt .0002 U NIl
$V-on M/U/.. In,,,'flcl.nt S..,lo or O...olv.. "-,.,. ",,01,... ..., r.""..,.4.
swoon 04/05/" .0500 U .02110 U .7.0 .00~0 U II. 'l4 . 10 .U. .0002 u' NIl
5..-05) OS/21/.' .0500 U " .02110 U II 2.61 " . 0010 U " .0'lJ2 II 11.10 II .181 II .0001 U V .0100 U "
SW.05) 06/26/.' .0500 U V .0250 U II .611 V .0050 U II .100 U V 10.50 V .418 II .0001 U V .100 U II
5W-05) 01/"1.' DAY
sWoon 08/15/.. .0500 U V .0250 U " ._54 V .0010 U II .100 U Y 26.40 V .51. V .0002 U V .100 U V
SW-051 0"20/.' .0500 U V . OliO U V J.II " .0050 U II .100 U I II. 50 V .4H II .0001 U V .100 U II
5W-05) 10/12/.' .0500 U V .0250 U V 2.1. V .0010 U II .100 U V 'l4 . 10 V .401 II .0001 U V .100 U V
swoon 11/071.' Dote not rat racllvl"
5w-on 12/15/.. Ooto not ,ot rlc.lvld
swoon 01/111.0 Oat. not ,ot rlel'v.d
5..-05) 02/U/'0 o.to not ,ot rlcllvld
VAtUf QUA1II'fAS: HI - An"rta not reported U - An"ra.d but not ."Ict..
J - 'r.I.'" below d.'.ctton It.I' . . Pr..,..' '" '...rater, ~1....
DAIA VAIIOAIION QUAlfl(R5: 1"0 volldot'on qu011110r Indtc.to. d.t. h.. not boo" v.I'..'o..1
. - Ho'dS.., tt.. not ..t I - 18't..".- val...
II . 'ote, .,1'0 "ot I" .O-IZ~ ro",o
I - ReJected, A - .cc.pt.~I. .It- 4"al"'c.t.on8;
-------
'..,
8urface .ater
Diasolve4 Hetals 8..pling aesulta
8TATION 53
Statton O.te Hleaol 'oto..l- S.t.nluM Sllvor 5...1- Stront 1- 'h."I- fin "....,-
H_or S...lod (Nit. dl... (II t. ..... (Sot. dl... (Alt. ..... (Not. ..... (Srt. ..... Int. .,... IS,,). .1... (' t. .....
.,/1 .,/1 _,/1 ../1 ../1 -,/1 ../1 ../1 ../1
.--------- -.-.--- ..._--.----
$\1-051 07/21/17 0.0' U .. HII 0.01 U IU 0." .. .. 0.01 V
$\I-on 06/11/11 .0.0 V .... .005 U .010 V 20.10 .117 .10 V .. .010 V
$V-051 O6/U/1I "..uffle 10'" 5...10 or Ol..olvod "-t.l. A...I)'... .... .......to..
$\I-on 04/05/11 .0.00 U III .0050 U .0100 V 11.20 HII .0100 U HII .0500 U
SII-051 OS/21/11 .0.00 V II III A .0050 V II .0100 V A ".'0 " IV " .0100 U II .100 V " .0100 V "
sil-on 06/1'/8' .0.00 U " III " .0050 U " .0100 V ., 17.'0 " .78' " .0100 U " .100 U It .0100 V .,
$V-on 07/11/8. OIlY
$\I-on 08/15/11 .0400 V " 5U " .0050 U " .0100 U A ".10 IU ., .100 U II .100 U ., .0500 U .,
$\I-on 0./20/11 .0.00 U II IU II .0050 V II .0100 U " 11.'0 " IU II .0100 V " .100 U A .0500 U A
$V.on 10/12/8' .0.00 U " 5U II .0050 U " .0100 U ., 17.50 " .,.. " .0100 U " .100 U ., .0!lOO U "
SII-051 II /07 /11 Oat. not ,at rac.'vad
S"-051 12/15/8' O.'a n.' ,a' race Iv."
SII- on 01/17/10 08\0 "ot ,at raeel"e.
SII-051 02/U/1O Ooto "0' rat racelv.'
VAlUI QUAtlfl(AS: HA - Afta.,t. no' report ad U - An..,..d ~ut not ..tacta'
J - Pre.ant ba'ow detactto" ,..tt . . Pr.....t 'ft '.~ar.tarr .,...,
O~I~ Y~'IO~IION QU~'fl(AS: (No ..lldotlon quoll'lor Indleoto. d.,. ho. not boo.. volldot.d.t
. . ....18.... t'" "0' ..t ( . I.' ,..'.4 V8 ,...
M . lotch 0"'0 not I.. 1O-12a1 ro..,o
. . ..Ject..; A - Accapt..'a .It. ~u.I'flc.t'on..
" . ".ltd
..
-------
STATION 53
5,.'10"
H"".r
SW-OS)
sw.on
sw-on
SW-OS)
sw.on
sw.on
sw-on
sw.on
sw.on
sw-on
swoon
sw.on
sw.on
SW-OS)
0...
So....lod
... --"-_..
01/21/.7
o./n/..
o./n/88
04/05/..
05/n/..
06/"/"
07/1./..
0./15/..
0'/20/.'
10/12/..
11/07/..
12/IS/"
01/.,/.0
02/ U/'o
IInc
Un). dl...
.../ I
.'___0" - ----
0.02 U
.OJ"
In,..fflclon.
.0200 U
.0200 U R
.0171 A
ORY
.0200 U R
.0200 U A
.0204 A
Surface Water
Dissolved Metals Sa.pling Results
5...10 or Ol"olvod Ho.ol, Anoly"o nO' roq..oo.ed.
DI'. not rot rec.lved
0... ..., '0' rocelvoel
00.0 no. ,.. roc.lved
Dlta not ,0' rocelved
VAIUf QUAllflfRS: "A - An.I,.. no. ropor..d U - Anol,.od .... "0' d...c."
J. Pro....t ..'0. 4otactton If.'t . . 'ro....t IR '."r...r, ~I.R.
DAtA VALIDAtiON QUAlflfAS: INo .olido'lon quollflor Indlco,o, do'o hoo no. bo.n volldo.od.)
. - IIoldln, tI- no' -. I( - htl_... wel..o
N . '..ch 0,1'. "0' In 80-1201 r.n..
. - a.Joctod; A - Ace.pt.". .tt~ _waltftcatton,;
.
v - Voltd
-------
Surface .ater
Dissolved Hetals Sa.pling Results
SOUTH WALNUT CRBBK
Stetton o.t. A 'u..I nUflil A"tl_lIr Ar..nte I.rl.. l.rrlll.. e.....I.. e.lcl.. e..,.. ehr_l-
N-.r 5..... led (All. diu. (5"1. .1... (A.I. ..... (1'1. ..... (hI. ..... (Cdl. .1... (Co). .1... (e'l. .1... (er). .....
.../1 "/' "'9/' "/' ../1 "'/' "/' "/' "/'
.-.--'---- .------.--.- . -- --" - --- -'..---
$W-OSI 07/21/87 0.2 U "" Nil 0.22 Nil NI IU III 0.01 U
$W-051 06/'0/" 0 . 200 U 0.010 U 0.010 U 0.200 U 0.005 U 0.005 U III III 0.010 U
$W.056 Ol/U/8. .200 U V .0100 U " .0100 U II .U5 V .oon " .0050 U I IIJ V IU v .0100 U "
SW.OSI 05/11/8. .200 U I .0100 U " .0100 U V .10' V .0050 U " .0050 U I 10. II IU II .0100 U II
SW.056 06/07/8. .200 U " .0100 U V .0100 U " .100 U " .0050 U V .0050 U II 118 " .100 U II .0100 U II
SW.OSI 07/82/8' 0.,. 110' '0' rocohod
SW-OSI 08/0./8. .200 U .0100 U .0100 U .1)2 .0050 U .0050 U 121 IU .0100 U
SW.056 0'/"/8' .200 U II .0100 U " .0100 U V .111 V .0050 U " .0050 U V 10. " IU " .0100 U II
sW.OSI 10/18/11 0.,. ''0' ,.t received
SW-OS6 11/15/8. 0.18 "0' ro' race Iv.'
SW,OS6 82/11/8. 0.18 "0' rot recelvael
SW. 056 01/25/.0 0.,. not ro' rac.tv.d
SW-OSI 02/22/" De', not "0' rec.l"ad
SW-OSI 0)/21/90 0... "0' '0' recel"ael
sW-OIO 07/21/87 0.2 U Nil Nil 0.1 U Nil Nil II' NI 0.01 U
"'-010 11/11/.7 I"...ff Ie lo"t So..lo or DI..olv.d Hoto'. ""01...,. ..0' r..uo.'o..
SW-OIO 07/01/88 0.200 U 0.010 U 0.0'0 U 0.100 U 0.005 U 0.005 U 105 "" 0.010 U
SW-OIO 0)/11/11 .200 U II .0100 U II .0100 U " .100 U " .0050 U " .0050 U I 10.10 II IU II .0100 U I
SW.OIO 0'/11/8' .200 U I .0100 U " .0100 U V .200 U " .0050 U " .0050 U I ".10 II IU II .0100 U II
SW.OIO 05/11/19 .200 U I .0100 U V .0100 U V .100 U II .0050 U " .0050 U I 70.10 II IU V .0100 U V
SW-OIO 05/15/89 .200 U I .0100 U V .0100 U' A. .100 U V .0050 U " .0050 U I 70.70 V IU V .0100 U V
SW.OIO 06/0./89 .200 U II .0100 U V .0100 U II .100 U A .0050 U " .0050 U I ".M A IU V .0100 U I
SW-OIO 07/01/8. .200 U " .0100 U V .0100 U " .100 V .0050 U V .0050 U V III V IU V .0100 U V
$W-OIO 08/0J/8. .200 U V .0100 U A .0100 U V .100 U V .0050 U I .0050 U II ".10 V IU V .0100 U V
SW-OIO 09/11/8' O.U 110' ro' rec.lved
SW-060 0'/11/8' 0.18 "0' rot recet".d
SW'OIO 10/0'/89 .0)00 U V .500 U V .0020 U V .181 V .0020 U V .0010 U V ".10 V .0010 U V .0200 U V
SW.OIO 11/01/89 0... not ..., received
SW.060 11/06/8. O.t. 110' ,ot rec.t.,.d
SW.060 U/0I/89 O.U lIot rot rec.'v.d
5W.060 01/2J/.0 0.,. "0\ r" race'v.d
5W.060 02/0'/'0 0... not ..at rec.' "ad
5W-060 OJ/U/'O Oa'a not r" rece'v.d
SW.061 01/22/87 0.2 U Nil Nil 0.2 U Nil Nil JO.I NI 0.01 U
V"lU£ QUAllfl£IIS: Nil - A".I". "ot ropor'od U - A"ol"od but lIot dotecto.
J - 'r...'" below d.'.ct'Oft "..tt 8 - Pr..,nt 1ft '.~.r.'.r, ~'.ft'
OAIA VAIIOA"ON QUAlf,£AS: rNo vo"do.lo" quoll'l.r I"dlcolo. do" h.. 110' booll v."dotod.1
. - Noldl.., tI- lIot _t [ - [.tI_hd v.'uo
N - 'otch .,1'0 "ot III 'O-II~ r..,O
. . ReJecte.; A. Accept..'. .tt' ~u.'tfte.ttoft.;
v - V.1I4
.
-------
f
--
surtace .ater
Dissolvect Metals sa.pling Results
SOUTH WALNUT CRBBK
Stltlon 0"8 Cobalt Copper Iron L..d lIth'- Me,,,..... ..."....... Mercllr" It<> , ,......-
"....bar S_'ed (Co). d'... (Cu). ...... (Ie). dl... ("). ..,... (L'). ...... (lit,. ..,... (""'. ..,... (lit,. ..,... (Me). ""e.
-,/' "/' "/' "/' -'/' "/' ../1 ../1 ../1
--_.- ----- ------- ---- ---- -------- --- ---
$\1-05' 07/21/87 0.05 U 0.021 U 0.1 U 1M l1li 21.1 0.227 HR 0.04 U
$\1-05' 06/JO/.. 0.050 U 0.015 U O. 100 U 0.005 U l1li U 0.011 U 0.0007 1M
$\1.051 04/U/8. .0500 U V .0250 U A .U7 A .0050 U V .01lJ V 21. 10 V .841 A .0001 V .0245 A
$\I - 051 05/11/8' .0500 U A .0250 U A .100 U V .0210 U A .0100 U V I'.JO " .185 " .0001 U II .8100 U V
511.051 0./01/81 .0500 U V .0250 U A .100 U A .0050 U A .100 U II 18.10 A .418 A .0001 U " .100 U "
511.056 01/1l/8I 01'1 not )'.t received
$\1.051 08/0./81 .0500 U .0250 U .100 U .0050 U .100 U 22 .550 .0002 U .100 U
$\1.05' 0'/14/81 .0500 U V .0250 U V .100 U V .0050 U A .100 U V 11.40 V .... " .0CI02 U " .100 U V
$\1.05. 10/18/" 0.,. not YI' receev.d
$\1.056 11/15/81 0.,. nol r.t racelved
511.056 12/ II/II 0... nol rei rlc,'ved
511.05. 01/25/.0 oa'l not )'.t rlc.lved
511.051 02/22/.0 0"1 not rat rlce'w.d
$\1-051 OJ/21/'0 0"1 not ,at received
SII-060 0,/21/., 0.05 U 0.025 U 0.1 U ... Nil 11.2 0.015 U NA 0.04 U
$\I. litO 11/11/81 "..,,'ftc'I.., S..,,1. or DI.lolved "",1, A"I'.'" ".t r...e...".
511. litO 01/01/.. 0.050 U 0.025 U 0.100 U 0.001 U Nil 11 0.015 U 0.0001 U l1li
SII.IItO OJ/II/8I .0500 U A .0250 U V .100 U V .0050 U A .100 U V 15.JO " .0150 U A .0001 U " .100 U V
$\1.060 OJ/II/8I .0500 U A .0250 U " .100 U " .0050 U A .100 U " 14.'0 " .0150 U A .0001 U " .100 U "
511.010 05/15/11 .0500 U A .0250 U A .100 U A .0010 U II .0100 U " 11.80 " .0211 " .0001 U II .0100 U "
SII-IItO 05/15/81. .0500 U II .0250 U II .100 U II .0010 U II .0100 U V 11.70 " .0240 " .0001 U II .0100 U "
511. litO 01/0./11 .0500 U A .0250 U II .100 U " .0010 U " .100 U " U.70 II .0241 " .0CI02 U ., .100 U .,
$\1-010 07/01/11 .0500 U V .0250 U A .100 U A .0050 U ., .100 U A II ., .01110 U ., .0002 U II .100 U A
$\I.IItO 08/0J/II .0500 U " .0250 U A .100 U ., .0010 U II .100 U ., 16.80 .0150 U II .0001 U ., .100 U "
SII.OIO 09/11/11 0.1. not ye' rlc.lvld
$\1-060 0./11/8. De" nol ret receIved
$\1-010 10/OJ/II .0200 U V .0200 U V .OJ02 A .0054 A .0200 A 16.50 V .0100 U A .0002 U A .500 U V
511-1It0 11/06/11 Oat. not 1'" received
511.060 11/01/8. 0.,. not ya' rle.'vld
511-060 12/01/11 011. nol ret rlcllved
SII.OIO Ol/U/.O 0.,. not "It recetved
$\1.060 02/01/.0 0... ..ot ret recetved
$\1-060 OJ/12/.0 0... not ret recetved
SW.061 01/22/87 O.O!i U 0.025 U O. t8 l1li Nil 5.0 U 0.017 NA 0.04 U
VALUE QUAL If lEAS: HA - An.lrle nol reported U - Anelr.ed .ul not "etecte"
J. 'r..ent b.'ow d.'.ctton ,.." . . 'r...ftt In 1.~or.ter, ~t.R'
DA'A VAliDAtiON QUAtfIIAS: CHo v.ttd.,ton qu.tlfl.r Ind'c.'.. d.'. h.. not b..n y.t'd.,...)
. . ...I4IIt.., 'I.. not .., [ . [.'t..'.4 ".Iu.
N . '.tc. .",. not ,.. eo.IZOS r....-
. - ..Ject.-; A. Acc.pt..,. wtt~ ~u.'t"c.tton..
-------
surface water
Dissolved Metals Sa.pling Results
SOUTH WALNUT CRBBK
Statton o.t, Nlc'" Pot...I- S.I.nluM $Ilver 5..1- $tro..t'- '''.111- It.. V...."-
N-or 50'" 'ad (N'). dl... (II ». d''', ($e). dl... (A,). dl... (1Ia). dl... (5r). d.... (tI). dl... (5..). dl... (" ». d"..
../1 ..II "'8/1 ..I' ..I' 891' ..I' ..I' ..I'
--....----..-- ..--.,..-- ---- -- ----.--
$\1- 056 07/2"'7 0.04 U NIl Nil 0.01 U 60.5 0.67 NIl NIl 0.05 U
$\1-056 "/JO/,, 0.040 U 5.0 U 0 . 005 U 0.010 U 51 0.' 0.010 U NIl 0.010 U
$\1-051 04/U/" .0400 U II 5U A .0050 U A .0100 U , &3.10 V IU V .0100 U II .100 U V .0100 U V
5W-On 05/11/" .0400 U II 5U II .0050 U " .0100 U " U , IU , .0100 U " .100 U , .0100 U V
5W-On 06/011" .0400 U A IIU A .0050 U A .0100 U A 49.70 V .574 A .0100 U " .100 U , .0500 U ,
SW - 056 071121" 0.,. not yet. recet.e.
5W.On 08/0"'. .0400 U 5U .0050 U .0100 U 57.60 IU .0100 U .100 U .0500 U
SW.056 0"16/" .0600 U A IIU A .0050 U A .0100 U A 41.'0 V IU V .0100 U V .100 U V .0500 U V
SW.OS6 10/1"'. 0." ..ot ,at r,c.'.8d
SW.OS6 11/15/'. Do" ..ot rot rec.'veel
SW.OS6 Il/I./.. Data ..ot rot rec,'.ed
SW-OS6 Ol/U/.O 0... ..ot r.t recetv.'
$\1.056 02122/10 0... ..ot r.t recet"..
5W-056 OJ/21/.0 O.t. ..ot ,.t rec.t"..
SW.060 01121/81 0.04 U Nil NA 0.01 U M.' 0.58 NIl Nil 0.05 U
5W-060 11/11/" I....., "clo..t S...,. or Ol..o'vod Mot.', A...I,... ..., .........'.d.
W.060 07/011" 0.040 U 5.0 U 0.005 U 0.010 U 26 0.6 0.010 U HA 0.050 U
$\1.060 OJII6/" .0600 U A IIU A .0050 U A .0100 U A 10 V ..8" V .0100 U A .100 U V .0100 U ,
SW-060 OJ/I6/" .0400 U A IIU A .0050 U A .0100 U A U.50 V .50' V .0100 U " .100 U , .0500 U ,
SW-060 05/151" . 0400 U II 5U II .0050 U " .0100 U " 10.20 V IU V .0400 U " .100 U V .0500 U ,
SW.060 051 III" .0400 U II 5U II .0050 U II .0100 U II 10.80 V IU , .0600 U " .100 U , .0100 U ,
$\1-060 01/0./.. .0400 U II au II .0050 U II .0100 U " '6.10 V IU , .0100 U " .100 U , .0500 U "
$\1-060 01106/'. .0400 U " au , .0050 U II .0100 U II 11.10 V IU " .0500 U II .100 U " .0500 U V
$\1-060 0810JI'. .0400 U V 5U V .0050 U " .0100 U , n.lo V IU V .0100 U " .100 U , .0100 U V
SW.060 09/11/" 0... ..ot r.t rec,'ved
SW.060 0" III" O.t. "0' rot received
$\1.060 10/0"89 .0200 U V .589 A .0020 U V .OJDD U V n.JO V .541 V .00JO U II V .0100 U V
SW-06D II 1°1/.. 0"8 not ret rec.lved
5W-060 II 106/8. 081. ..ot ,., rec.t".d
SW.060 12/01/" Dot. ..ot r.' "'II..d
SW 060 ollnl.o 0.,. not ,ot rec.lved
SW 060 02'0"'0 D.'. nol rot r.c.'","
SW.060 OJ/I2/1O 0... ..ot r.t ree.' .ed
SW 061 01122/81 0.04 U Nil Nil 0.01 U 11.' 0.02 U NIl NIl 0.05 U
VALUE QUAL If lEAS: Nil. "..ol,to ..ot roportod U . A..ol,.od b..t ..ot d.t.ct.d
J - 'r...n' ..10. ..'8ctlo" ".It I . Pr...n' In '...r.'.r. ~,...
OA'. VAtlDAtlON QUA' flEAS: ("0 vetld.' loft qu.lt'l.r Indlc.'.. d.'. hee not b..n y.II~.t...)
. . Ho'd'", U- ..ot _t [ . [.U_tod ...1...
N . '.tc" .,1'. "0' t.. 8O-llaI .....,.
. - a.J.ct.dl A. Accept._1. .t,~ 4w.ltftc.'tone;
V - V.lld
.
-------
SOUTH WALNUT CRBBE
St.tton Do"
NU8b.r So",,'od
$V-OSI 07'ZI,.7
$V-OSI u.,JO,"
$V-OS' 06' U,..
5W-OSI OS, ..,..
$V-OSI 0"07'"
5W-OSI 07'1'1'"
5W-OSI 08'0""
$V-OS' 0""'"
$V-OSI 10"""
5W-OSI ..,IS",
5W-OSI U, "'8'
5W-OS' ol,n,tO
SW-OSI Oz,zz,tO
5W-OSI OJ''lI'tO
5W-OIO 07'ZI,87
$V.U.O "'''''7
5w-OIO 07'01'"
5W-OIO OJ, ..,..
5W-OIO OJ, ..,..
5W-OIO OS,15'"
5W.U.0 05'15'"
5W-U.0 0"0""
5W-U.0 07'0""
5W-OIO 01'01'"
5W-OIO 0" ..,,,
SW-OIO 0""'"
5W-OIO 10,OJ,"
5W-OIO ..,u.,..
5W-OIO ..,u.,..
5W.OIO 12'0""
SW-OIO 01'2J,'0
5W-OIO Oz,o.,tO
SW-OIO OJ,U,tO
5W-061 07,ZZ'87
llnc
(Inl. dl..-
..'1
----.-
Dissolved
Surface Water
Metals Sa.pliDC)
Results
0.27
0.010
_OUI A
.0200 U .
.0.13 A
Data ftot ,at rac.'ved
.0Zoo U
.OJI7 A
O.t. not
00.. not
Ooto not
00" not
Oa'a ''0'
Ooto ..ot
0.5'
I..o..fflel...t
0.400
.nJ
.111
.248
.1.5
.600
. "I
.158
v
V
A
A
V
A
V
,a' recetvad
,ot roeolwolll
,ot roeolvo"
,ot roeoho"
,at rac.lvad
,at racetva.
50....10 or Olooolv.' "-tolo A..ol,o'o ..ot r..uooted.
0.'0 ftot ,at racalvad
0..8 no' ,at racatv..
.Z18 V
Oat. not ,at
Do" ..ot ,ot
00" ..ot ,.t
D... "0\ ,a'
Oa.. not ,a'
Do" "ot ,ot
O.OS
rac.lved
rac.l"a.
racat"ad
racelvad
rac.tv.ct
rac.'"ad
VALUE QUAL If lEAS. NA - Anol,t. "ot roporto' U - Anol,... b..t ...t lIIotecto'
~ - Pr..ont b.low 'otoctl." 11.lt . . Proo...t I.. loborot.r, bl..'
OAIA VALIOAIION QUAlfIEA5: (No volllll.tlo" ~..ol"I.r Indleoto. do.o hoo "ot boo.. vollditoill.)
. . 110'"1.. tI- ..ot _t I . loti_to' ..0'..0
N . 'otcb opl'. "ot I.. 10-1101 ro...
. . ..Joctolll, A. Aceoptob'o _Itb ~,,"II'lcotlo..o;
~
V - Vo""
-------
Surface Water
Dissolved Ketals SaapliDCj Results
SOUTH WALNUT CRBBIt
Statton Oat. A'uM'n... Ant 1_", Ar..nlc hrt- l.r,lll- C....t- Calct- Cut- Cllr_t-
H"".r Sa..I.. (AI), .1... (n), tit... (AI to ,t!... (I.), "II. (I.), .t... (Cd), ..... (C.), .tll. (C.), dtll. (Cr), "11.
89/1 -'/' I -./1 "/' "/' -./1 ../1 ../1 "/'
._- .... --..---- --------- -.---- -_.--- ----- --'
SW-~I 11/11/'7 I,,"ufftc I.", Sa..l. or Otllolv.d ...,... "".1,... "0' r..u.ot.d.
SW-OII 07/01/88 0.200 U O.MO U 0.010 U 0.200 U 0.005 U 0.005 U .. HII 0.010 U
SW.OII OJ/20/.. .200 U V .0600 U A .0100 U V .200 U II .0050 U A .0050 U II 27 II IV II .0100 V V
SW.OII 05/15/81 .200 U I .MOO U " .0100 U II .200 U II .0050 U " .0050 U I 10.10 ' IU , .0100 U V
SW-OII 01/0./81 .200 U , .MOO U V .0100 U " .200 U " .0050 U " .0050 U I 87.10 " IU , .0100 U I
SW. Oil 07/01/81 .200 U " .0600 U , .0100 U II .200 U II .0050 U II .0050 U II 10.10 ' IU , .0100 U II
SW-OII 06/0J/.. .200 U II .MOO U " .0100 U II .200 U " .0050 U II .0050 U II '7.10 II IU " .0100 U I
SW-OII 0'/11/" O.ta not rot rocetvo41
SW-OII 10/0J/.9 .OJOO U V .500 U V .0020 U V .In V .0020 U V .0040 U V 81.50 V .0010 U V .0200 U V
SW.OII 10/20/.. OIY
SW.OII II /01/.. D.ta "0' ,., roc.'''ed
SW - 011 U/OI/.. Da'. ..., ,., rec.t.,..
SW- 011 OliUllO 0.'. ".1 ,.t roc.t.,.4
SW-OII 02/0./10 Data "o1 ,., rocetv.d
SW- 011 OJ/12/.0 Oat. "ot ,., roc.t.,.d
SW.OII OJ/12/1O 0... "0' ,., roc 8 t va.
SW.IOI 06/JO/.. 0.200 U 0.060 U 0.010 U 0.200 U 0.005 U 0.005 U 12 III 0.010 U
SW-IOI O./IJ/.. O.t. "ot ,.t rae.Iv..
SW.IOI 05/11/" .200 U II .1H500 U " .0100 U V .200 U II .0050 U " .0050 U I '.n V IU " .0100 U "
SW-IOI 01/07/.9 .200 U " .0600 U , .0100 U II .200 V " .0050 U , .0050 U " 10.10 " .100 U , .0100 U II
SW-IOI 07/12/.. 0.'. "01 ,ot rocelved
SW-IOI 08/0./.. Oat. "., ,., rae.lv..
SW-IOI 0"14/" .200 U v .0600 V " .0100 U II .200 U II .0050 U " .0050 U II 7.72 " IU " .0100 U II
SW-IOI 10/1./.. De ta "ot rot racet"a.
SW-IOI 11/15/" Oal. "ot ,., rae.lv.'
SW.IOI 12/"'" Oat. "0' ret roc. tv.'
SW-IOI 01/25/90 De'a nol ,., roc.''''a'
SW.IOI 02/22/.0 Da.a not ,., rec.tveet
SW-IOI OJ/2I/90 00'. not ,.t rec.lvad
V"LUI QU"LlfIIIlS: HR - A"al". "0' r.por'.. U - "".1,... lIu' "0' d.'.c'..
J - 'r.I.'" 11.1.. ".'.c'lo.. It.lt . - 'r.a...' tIt 'a"'r.'.r, 111....
OAIA VAl IDA I ION QUAtfllRSI (Ho .all'.'I... .u.II'I.r tn.lc.'.. date haa "0' b.... v.I'''at...)
. . 1tI'4It... U- "ot .., [ - [aU-'.' valu.
II . 'a'cll .,111. "., t" eo-12a1 ra..,.
. - ..Jocto4& A - Acc.pt.~'. ...~ ~u."ftc.ttOft'i
v . V.".
(
-------
~
.,
Surface Water
Dissolved Metals ...pling R.sults
SOUTH waLNUT CREBK
Statton Olta Cob. It Copper Iron l.... lIU.I- "'8....1- Ma",...... Mercyrr IIoI,W...-
Nu.ber S.."... (Co). ell... (C..). .118. (h). d'... ('~)' ..... ClI). ..... (lit). . h.. C",,). ..... CIIt). ..... Clio). .....
89/1 ../1 I ../1 ../1 ../1 ../1 .../1 ../1 ../1
.----_.------- ... .-.--'--"-- ---- .-..----..- ---.- ..----
SII-OU 11/11/'7 I.....'tlel..., S..,~. or DI..ol..,8" H8t.l. "...1)'." ..., r""....'.".
511-061 07/01/88 O.OSO U 0.025 U O. 100 U 0.001 U "" II 0.011 U 0.0002 U ..
SII.OU OJ/20/.. .0500 U " .0250 U V .100 U V .0010 U " .100 U V '.'1 V .0'" V .0001 U V .100 U V
$11.061 05/15/.. .0500 U " .0250 U " .100 U " .0050 U " .0100 U V 11.10 " .0112 " .0001 U " .0100 U "
SII-OU 06/0./.. .0!lOo U " .0Uo U " .100 U " .0050 U " .100 U V 1...0 " .OJ" V .0002 U V .100 U V
$II-OU 07/06/.8 .0500 U V .0250 U " .100 U " .0050 U " .100 U " ".'0 V .OUO V .0002 U " .100 U "
$II-OU o./OJ/II .0500 U V .0250 U " .100 U " .0050 U " .100 U V ".20 V .0.15 V .0001 U V .100 U V
SII-OU 08/11/.8 Oa'a not ,at recetva"
$11-081 10/OJ/.8 .0200 U V .0200 U V .12J " .0020 U V .0200 " 16..0 V .0507 V .0002 U " .500 U V
SII-OU 10/20/" OIlY
$II-OU 11/06/" 0.'. not ret r.c.t".d
SII-061 12/01/.. 0.,. "08 ,., rece'v,.
$II.OU Ol/U/.O D... "0' ,., rec,'ve"
$11.061 02/0./80 0.,. ..01 ,., rac.tv."
$11-011 OJ/I2/.0 D... ..0' ,., rec.'v,"
$11.011 OJ/I2/80 Data not ,., rac.tved
$11-101 06/JO/88 O.OSO U 0.025 U 0.2 0.001 U .. 1.0 U 0.011 U 0.0007 ..
SII-IOI 0./ &J/II De,. not re' recet"...
$11-101 05/11/" .0500 u II .OUO U " .100 U " .0250 U " .0100 U V 50 V .0150 U V .0002 U II .0100 U V
$11-101 0./01/.. .0500 U II .02SO U " .115 " . 0010 U " .100 U " au " .0110 U " .0001 U II .100 U II
$11.101 01/12/11 D... ..0' )'.' recat"...
SII-IOI 0./0./.. D.'. ..., )'.' ree.tv.'
$11-101 O./U/.. .OSOO U V .02SO U V -100 U II .0010 U " .100 U V IMI V .0150 U V .0002 U V .100 U V
$11-101 10/1./.. O.h "0' rat rac.tv.d
$11-101 11/15/11 0"8 ".t ,., r.e.lv..
$11-101 12/18/.. D.'. ..0' ,., ..calv..
$11-101 01/25/80 Oa.a not ,at raca've"
511-101 02/22/80 0.'. not ,., receive"
$11-101 OJ/21/.0 O.h ..0' ,., racII",.d
VlllU( QU"llfl(IIS: "". "...I)'t. ..ot r.port... U . "...1"." but ..0' ..'.e'."
J . 'r...nt ..10. ~.'.c'lon 11.1' . . Pr...n. 1ft '.~.r.t.r, ~1...
OA'" VAlIO"'ION QU"lflfAS: (Ho v.lleI.tlo.. ~u.II".r ,.."Ie.'.. eI.t. h.. "0' b.... v.II~.'.".)
. . 1101.'.. 11- ..ot -, I - II"..,... u.lu.
N . '.'eh .,1'. "., I.. 8O-I,ga r.....
" - II.J.et.~. ". .ec.,'.~I. .I'~ ~u.I"lc.'lo...;
-------
8urface Water
Dissolvec1 Metals Sa.plinCj Results
80UTH WALNUT CRBBK
St.tton Dolo N'
-------
SOUTH WALNUT CRBBK
5'."0" 0.'.
N~bor So..lod
sw-oel
SW-O.I
SV-OII
SW.OII
SW-061
SV-O.I
SW-O.I
SW-O.I
$W-O'I
SV.O.I
SW-061
SW-061
sw - 011
5W-O.I
5V-0.I
$W-061
5V 101
sv- 101
SV-IOI
SV-IOI
$W-IOI
5V-101
SV.IOI
SV-IOI
SV-IOI
SW.IOI
SW-IOI
SV-IOI
5W- 101
... -- ---- --..-
11/11/.7
07/01/..
01/20/..
05/15/..
08/0./..
07/08/"
0'/01/"
0'/11/"
10/01'"
10/20'"
11/06/"
12/06/et
01/21/.0
02/0./.0
01/12/90
01/12/.0
06/10/88
04/11/89
05/11/"
06/07/"
07/12/"
08/0'/"
0'/16/"
10/1'/"
11/15/"
12/1'/"
01/25/to
02/22/to
01/21/.0
llnc
(In), dIU.
-fIll
Surface Water
Dissolved Metals Sa.pling Results
51"'0 or Oliiolvod Hotolo Anol"o'" not roquolto~-
Inlu"lelont
0.100
. 0.64 A
.0200 A
.1.1 V
.0200 U A
.0817 V
0.,. not ~.t rec.t"e.
A
.0J47
OIlY
Oat. not )'a'
0.'8 "01 re'
D.'. not rat
OltO not ..ot
Do.. not ..ot
0... not rat
0.010
0... not
.0200 U A
.0267 A
0... not ,.,
01" not ..ot
.0115 A
0.'. not y.'
Doto not ..ot
Oa'a not r.'
Data not r.'
Do" no' ..ot
Oa'a not rat
'8c81"8d
rec.l"e.
raca'".eI
raeat"ad
rac.tvael
racat"ael
y.t racatved
racelved
roeolvo'
raca'vad
rac.'ved
racat".d
rec:..I"acl
racelvad
raca'wad
VALUE QUALifiERS: HA - Anolrto not ropo,tod U - Anolr.od but not ~otocto'
J - Pr...nt b.low ..'.Cllo" ".., . - Pr...nt IR '.~r.t.r. ~,.".
OAf'" YAIIOA'ION QUAlfUAS: eHo va"datton q"."ftar t..dleat.. d... .... "01 b.... "."........)
. - Hotdl.., tI- lIot _t ( - htl_to' vol..o
N - tote" .,1" not In eD-12ft n..,o
. - AeJact.dl A. Accepl.b1. wte. 4w.I.'lc.elon8;
~
V - Volld
-------
'..\
Dissolve4
Surface .ater
Hetals sa.pling
Results
STATION 59
5'.'10" 0.'. AI-In- Anti....... Ar'.Ale hrl- 'orylll- [e..l- [elcl-
H_or Se..lod (All. ~he. (Sb). ~I... (AI). ~I... (Ie). ~I... (Ie). ~t... (C"). "I... (Ce). "t...
...'1 "'/' .../1 .../1 "'/' "'/' "/'
,
--- ---'----
SW-OS' 07/21/87 0.2 U . HR HR 0.2 U NA NA 122
SW-OS' 0'/01/88 0.200 U 0.010 U 0.010 U . 0.100 U 0.005 U 0.005 U 108
SW-OS' 01/20/81 .200 U . .0100 U A .0100 U A .100 U V .0010 U . .0010 U . 112 V
SW-OS' 05/11/81 .200 U . .0100 U II .0100 U V .200 U V .0050 U . .0050 U . ..10 V
SW-OS' 01/01/1. .2110 U II .0100 U II .0100 U . .2110 U V .0050 U II .0050 U V I" V
SW-OS' 07/01/81 .2110 U II . 01110 U II .0100 U A .200 U V .0050 U " .OOH U " 114 V
SW-OS' 08/10/" Dete not yot recetved
SW-OS' 0./11/8. .200 U V .0100 U A .0100 U V .200 V .0050 U A .0050 U " III "
SW-OS' 10/01'8' .0100 U A .500 U " .0020 U V .112 V .0020 U " .0040 U " 100 "
SW-OS' 11/01'" De.. not Jlet recet"ed
SW-OS' 11/01'" Oe.. ..ot Jlot received
SW-OS' 01'21"0 D.'. no' t'e' recel"ed
SW-OS' 02'0'/10 De.. not Jlot received
SW-05' 01/12/10 Do" not Jlot receive"
[oel-
(Ce). "ho.
"'/'
NR
NR
IU "
IU ..
.100 U V
.100 U V
IU "
.0010 U V
"AIUE QUAlifiERS: HR. AnolJlto not roportod U . Anelyled but not ~ot..t."
J - Pre.en' ~.'o. 4eteettoft 'I.It . . Pr...ftt 1ft '."r..er, .,...
DAIA VAliDAtiON QUAlfIIRS: (Ho vellde.lon quellfler Indlcete' de.e he. no~ b.... v.lld.to~.1
. - He'''I''1 tl... ..ot ...t I - letl..,o. v.luo
N . I.t.- 1,1.0 n.t In 80-1201 ro.,.
. - .0Jectod; II. Accopte.lo .It- .uell,tcetlonl; ". "oll~
~
Chr_l-
(Cr). .1...
.../1
0.01 U
0.010 U
.0100 U .
.0100 U "
.0100 U V
.0100 U .
.0100 U V
.0200 U "
-------
~
.
8urface Water
Dissolved Metals 8a8plinq Results
8'1'&'1'1011 59
Ste.lon D.'. Cob. It Copp.r Iron l.... lfU,I- ...."..,- .....,...... "'rct8r, "'1,.......-
_.r S..,I.d (C... d.... (C.... ...... (h). dl... ('b.. "I... (lI). ...... (..... "I... (""). ..h.. (..... "I... (Me). ..h..
.,/1 ..,1 .../1 ..II ..II ..II ..II ..II ..II
--.---- ------- ---- ----- --
5'1-05' 01121/81 0.05 U 0..11 U 0.1 U HI HI 24.4 0.011 U HI 0.04 U
W-OS' 01/01/" 0.050 u 0.025 u 0.100 U 0.0011 U HI 20 0.011 U 0.0002 U HI
sw-OSt OJ/20/" .0500 U II .0250 U II .100 U II .0110 U " .100 U II 11.10 V .0"4 " .0007 " .100 U II
sw-OS' 05/111" .0500 U " .0250 U " .123 ' .01110 U " .0142 ' U.20 ' .0JIt V .0001 U I .0100 U ,
sw-oSt ""08/" .0500 U II .02" " .100 U " .00110 U I .100 U a 20.)0 ' .0150 U " .0001 U V .100 U V
w.os, 07/""" .0500 U , .02110 U , .100 U " .00110 U " .100 U V 22.10 ' .0411 V .0001 U , .100 U ,
sw-oSt 08/10/" 0." ''0' ,., rec.'ved
sw-oSt 0""'" .o~oo u v .ono u v .100 U v .0050 U v .100 U A 'IS. JO v .0150 U A .0002 U v .100 U A
sw-oSt 10/01/" -0200 U v .0200 U II .OJ61 " . 0020 U , .0250 " 11.10 ' .0100 U , .0001 U " .SOD U v
sw-os, 11/061" 0... not yet rec.lved
swoon 82/06/" 0... ..0' ,., racetved
SW-OS' 01/21/'0 0... nol ,., rece'ved
sw-oS' 02/0'1'0 Oa.. not ret rec.lved
SW-OS' OJ/12/'0 0... ''0' ,., rec.'ve.
VAlUi QU"ll'IIIS, HA. "".1". "., r.,ort.d U . A".I,.... but "ot ...toct."
J . Pr.'...1 ~.,o. 4.,.cllo" 11.11 . - Pr...... tft 1'''r.t.r~ ......
DAIA VALIDATION QUALfIIAS: (No ..1'''.'10'' qu.II'I.r I,,"'c.'.. d.'. h.. "0' b.... ..Ild.'.".)
. - Mo"I", tl.. "ot ..t I . I.tt..t" v.'u.
H . ..tc' .",. ".t t. 1O-11Oa r..,.
-------
surface Water
Dissolve4 Netals SaapliD9 Results
STATION 59
Statton o.to Hlchl 'ot... t... S.'.n'... II "'or loell- Strollt 1- '''0111- ,,,. Vo..oell-
H_er ...,Ioel CHII. 41... CI ). ell... (50). elh.. (A,). elho. Clio). elln. (Sr). elln. (n). elho. (S..). elloo. (V t. clho.
-.1' ..I' ..I' ..,1 ..,1 ..I' ..I' ../1 ../1
--.-..- _.-- --L- -.---.-
IV-OS' 07/21/87 0.01 U ; HI HI 0.01 U ..2 0.71 .. .. 0.011 U
"'-0.' 07/0'/18 0.040 U 5.0 U 0.005 U 0.010 V 21 0.' 0.010 V .. 0.0110 V
IV-OS' 01/20/" .0400 V V 5V A .0050 U A .0100 V V ..10 V I.., V .01" U . .100 V 'I .0100 V 'I
$\/-05' 05/''''' .0100 U . III . .0050 U " .0'00 V " I8.JO 'I IU V .8100 V " .100 V V .0IlOO V 'I
5W-OS. 01/08/" .0100 V V III " .0050 U A .0100 V 'I 12.10 'I ...1 " .0100 V V .100 V 'I .0500 U V
$\/-051 0'/011" .0100 V 'I 5U " .0050 U A .0100 V A n.40 'I ...1 A .0100 V A .100 U V .0IlOO U 'I
$\/-OSI 08/'0/" Ooto IIOt yot recetve"
5W-OS. 0"1'/11 .0100 U I SV " .0050 U I .0100 U V n.40 V IU A .0400 V 'I .100 V " .0500 U II
$\/.05. 10/01/" .0100 U 'I .750 " . 0020 V II .0100 U 'I 10.40 'I .142 'I .0010 V 'I IU V ...00 U 'I
5W-OS. "'Oll" Ooto IIot yot received
5W-OS' 12/01/" Ooto IIOt yot recetv."
Sw-OS' 01/21/.0 Ooto IIot yot recetv..
IV-OS' 02/0"10 Ooto IIot rot rec.tv.ct
5W-OS' Ol/U/" Ooto IIot rot received
VALUE QUALifiERS: HI - Anolrto not roportod U - Anolr.od but IIot elotocto'
J . 'r...n' ~.,ow detect ton 1..It . . 'r,'.R' 1ft 1.~r.t.r, .,...
OAIA VALIOAIION QUALfIER5: (Ho v.lldotloll quollffor Indlcot.. dot. ~oo ..ot b.o.. vo'idoto'.)
. - Mo'ell.., tl.. IIot ..t I - 10tl..t.eI vo'vo
" - 'otc" 0,1'0 IIOt I.. ".12a1 ro..,o
. - .0J.ct.eI. A - Accopto"'o -I'" .vo'I'lcotloll'; V - Vollel
~
-------
STATION 59
St.'ton O.t.
N,".r S..,I.d
SV-05'
SV-05'
SV-05'
5v-OSt
511-05'
511-05'
SV-05'
511-05'
511-05'
511-05'
5V.05'
5V.05'
5V.05'
511-05'
- .------.-.-
01/21/81
01/01/"
01/20/8'
05/11/8.
0./08/..
01/oa/..
08/10/8.
0./18/8.
10/01/.'
11/08/..
11/08/8'
01/21/90
02/0./.0
01/12/.0
Iinc
(In). diu.
../1
. - ------
0. )I
0.200
..21 "
.0200 "
. "' II
.0111 II
00.. no' r.' r.c....d
.2J2 V
. IN II
0... no' r"
d... no. r"
d... nol r"
De.. not ..at
D... nol ,..
recetyed
rec.'".'
received
rec.'ved
recet"ed
.. ,
Surface Water
nissolve4 Metals saapling Result.
lI"lUE QUAlif1ER5: HA. "n.I,.. not r.port.. U . "n.I,... but .0' ....ct..
~ . 'r...nt b.low ....ctlon '..1. . . 'r...nt ,. ,.bor.t.r, bl..,
OA'. VALIDAtiON QUAlfIIAS: (No v8"4attoft qW8Itf'.r '"dlca... d.t. ~.. not b.eR V8"..'...)
. - ...,.,., tI- no' -. I . htl_t.. ..'u.
N . ,.tcb .,1'. n.' I. eo.11Ga r..,.
. - ..Ject... A. Acc.pt.~'. .It. ~u.'tf'c.t'...;
.
V . 11.11.
-------
Dissolved
STATION 63
5'8tlo" Det. "'...n.... Antf-"r Ar..n'c
"_er 5...1.41 (AI). d.... (511). dh.. (A.). d....
rat/ I ..II .,/1
-------- --- - -.-- ---
IV-on 01124/81 0.2 U .... HII
.,-on 01/HI" o.on o.!>oo U 0.00)
.,-on 0)/28/8. DAY
IV-on 05/12/.. DAY
IV-HJ 01/21/.. DAY
IV-HI 011"/" DAY
IV-on 08/11/" DAY
IV-on 0./15/.. DAY
IV.on 10/04/" DAY
IV-on II IOJ/8. DAY
IV-OI) 12/01/8. DAY
IV-on 01/05/.0 DAY
IV-on oZ/oz/1O DAY
Surface .ater
Ketals Sa.pling
Results
ler'- I.rrllt- c.....- C.lc'- c...- CII.....-
(I.). ...... CI.). ..... (c..). ...... CC.). ...... (c.). ...... CCr). ......
..II ..I' ..I' ..I' ..I' ..II
---- --
0-1 U "" HIt III HIt 0.01 U
0.104 O.OOZ U 0.004 U ".0 HIt 0.010 U
VALUE QUAll'IEIIS. "". A...lr" n.t r.,o.t.d U . An.lr..d lIut ...t ...t.ct"
J . ,...."t 11.1.. ..t.ctlo.. II.lt I . 'r..."t I.. 1.lIar.'.r, III...
DAIA VAlIDA'ION QUAl'IEAS. (Ho valld.tlo.. qu.l.fl.r 'ndlc.t.. data h.. not II.... ..II..t...)
. . ...,...., tt- ...t -t E . hU-'''' ...'u.
N . I.'ch .,1'. ..., .. IO-I~ r..,.
II . II.J.ct.., A. Acc.,tall'. ."" .u.,.f'c.tlon.; V. Va""
"
-------
Dissolved
Surfaae .ater
Hetals ...pling
STATION 63
St.tlon 0... C.b.1t C.".r Iron L...
"...It.r 5.... '.eI (Co), elt... (C..), .18.. (r.), dt... ('b), .18..
../1 ../1 ../1 ..I'
--- ---- -----
SW-"I 07/24/.7 0.05 U 0.02' U O. I U NIl
SW-"I 07/"/18 0.020 U 0.020 U 0.062 0.005
sw-on 01/28/.. DAY
SW-on 05/12/" DAY
Sv-OU "/21/" OIlY
sw-on 07/1'/" DAY
sil-on 08/11/" DAY
SW-OU 0./15/.. DAY
SW-OU 10/04/" OIlY
SW-"I 11/01/.. DAY
511-0111 12/01/" DAY
511-0111 01/05/'0 OIlY
SW.OU 02/02/'0 DAY
VALUE QUALlflfRS: NIl - An.lrt. not r.por'.' U - An.lr..' b.., .., '.'ee'"
J - 'r....' bel.. ..t.ctton II.lt . - 'r....' I. I.ber.'.rr bl...
DATA VALIDATION QUAlfIERS. (No ...II'.'lon ~u.II'I.r Indle.'.. d.t. h.. no' b.,. ...11'.'''..
U'hl-
(U), .18..
../1
Resulta
".."..,-.-
(Ht), ell...
../1
Nil
Itll
".0
n.1
......."...
(....), .1...
..I'
O.HJ
0.4.1
..
Itorcurr
(Ht), ell...
"/'
NIl
0.0002 U
. . ItoI.I., 'I.. .., .., I - I.'t..,.. ...1...
It - Io'e. .,,,. n.' I. 8O-12ft re...
. - I.Joet..1 A - Aeeo,'.bl. wi'. ~u.llfleo'I..'1 V - V.'I'
.
Itolpllclon-
(Ito). .t...
../1
0.04 U
-------
STATION 63
St.tlon 0.'. Hld.I Pot... I..
H_.r '_'.d (HI). dl... (K ). dl...
../. ../.
..------ --- -----
SW-NJ 07/2./.7 0.0' U ...
SW - 0.. 07/08/" 0.020 U 1.'4
SW- 0" OJ/28/" DR'
sw-on 05/12/.. DR'
sw-on 08/21/11 DR'
SW-OIJ 07/11/.. DR'
sw-on 08/11/" DR'
sw-on 0./15/.. DR'
sw-on 10/04/.. 011'
sw-on II/OJ/II 011'
$W-NJ 12/01/" 011'
SW-OIJ 01/05/10 DR'
sw-on 02/02/'0 011'
Surface .ater
Dlssolve4 Hetals S..pllDg aesult.
S.I.nl- Sn".r Sedl-
(h). .11... (A,). ..... (Ite). .....
8fI/' ../. ../1
-----
H8 0.01 U 110
O.OO~ U 0.0)0 U 102
Stn.."- '''''1_ ''.. V...."-
(Sr). ..... (II.. ..... (In). ..... (V). .....
../. ../. ..'I "/1
---
1.07 .. .. 0.08 U
1.28 o.JOG U .. 0.01' U
VALU[ QUALlfl[AS, NA - An.I,t. not r.port.d U - An.I,..d hut ...t d.'.c'.'
~ - Pr.'.At "'o. ~.'.ctfDR It.ft . . Pr....t f. '...r.'.r, -....
DATA VALIDATION QUA"I[AS, ("0 ".II'.tlo.. _u.II'I.r Indl..t.. d.t. ~.. not h.... ..II..t.'.)
. . 118..1.. U- ..., -, 1 . 1."-'" ".Iu.
N . '.'.h opl'. Re' t.. ...llOa r..,.
. . '.J.ct.', A - A...pt.h'. .1" ,..II.I..tl..... V - V.II.
~
-------
.
.
Dissolved
surface Water
Ketals sa.pliDCJ
Results
STATION '3
5'."0" 0.'. Zinc
H_er s...lod ."'). d I...
../1
--"'--------' .-.------
5II-OU 07/24/87 0.01
5II-OU 07/04/88 0.02'
SW-OU 01/2./11 DII.
SW-OU OS/I2/11 DII.
511- au 04/ZI/8. DII.
SW.OU 07/11/11 DII.
sw-oU 08/11/11 DII.
511- au 0'/15/11 DII'
5II-OU 10/04/11 DII.
sw-oU 11/01/11 DII'
SW-OU 12/01/11 0..
SW-OU OI/OS/tO DII.
5II-OU 02/02/.0 DII'
VALUE QUAllfIEAS: HA - Anoly'o not roportod U - Anoly.o. ~yt ftOt .otoct..
J - 'ro.on' '010. .otoctlo. 11.lt . . 'roooftt 1ft 'o"rotor, .10.'
DAIA VALI~'IOH QUAL'IEAS: INo .oll.o'lon quollflor Indleoto. do'o ~o. ftot boo. volt..to..)
. . Me,.t", ,,- ..ot -t I . lo"-t.. ".'''0
" . ..tc' 0,1'. n.' t. 8O-1~ r....
-------
STATION 6.
Stet 'on Pete
~.r S.~I..
$W-O"
$W-O"
$W-O"
$W.064
SW-Ofl
SWo064
SW-064
sw- 064
SW.064
SW 0 064
SWo064
SW - 064
$W-064
.-.---
0,/22/.'
01/01/..
03/30/"
OS/22/"
01/21/..
01/11/"
08/11/"
0./20/..
10'04'"
11'0""
Il/OI,..
01'05"0
02/02'10
AI-In-
(AI). dl...
..., I
-.. ---------
0.2 U
0.04'
DAY
.200 U II
.200 U "
DAY
l1li,
DA'
DA'
DA'
DAY
DRY
DA'
surface Water
Dissolved Metals Sa.pling Results
Antt-..~ Ar._nte ..rt- hr.II'- C...I- C.lcl- c..,- Cllr_'-
(nl. d'... (A.). .1... (1'1. d'... (I.). d'... (Cdl. d'... (C.). dl... (c.). d'... (Cr). .....
../1 _.'1 "/' ../1 ../1 "/' "/' ../1
...--
Nit H" 0.1 U HI .. IS.' .. 0.01 U
0.500 U 0.002 U 0.101 0.002 U 0.001 U II.' .. 0.010 U
.0100 U " .0100 U " .200 U V .0050 U V .0050 U " n.IO IU " .0100 U "
.0100 U " .0100 U " .100 U V .0010 U V .0010 U V 71." V .100 U V .0100 U "
VAlU[ QUAll'II"S: HI. A...I~t. not r.port.. U . "n.I~..d ...t ...t ..t.ct..
J. 'r.....t ...10. d.t.ctlo.. I'.'t . . 'r....t ,.. I....r.t.r. "I...,
DAIA VAllDAIION QUAI'lfAS. (No v.II..'lo.. ~u.II'I.r 'nd'e.',. d.,. h.. ..0' ...~. v.I,..t...)
. . Heldt.. tt- not _t I . hlt_ted ..1...
M . ..tell .,1'. n.t ,.. IO.II~ r....
a . ".Jeeted, A. Aeee,te..l. .'tll .u.I"'e."o"., v. v.I'.
fJ
-------
ST".,IOII '4
Statton 0... Cobolt
M""er S....'.d Cc.t. dl...
"/'
SW-014 0"12/11 0.05 U
SW-H4 0"0"88 0.010 U
SW-H4 OJ/JO/.. 08'
SW-014 OS/22/.' .0500 U V
SW-014 04''''.' .0500 U V
SW-014 0""'.' 08'
SW -014 0'/1) ,.. 08'
SW-014 0'/'0'" 0111
SW - 014 10'04'.' 08'
SW-Ot!4 11/0'/" 0111
SW - 014 12/01'8' OA'
SW-014 01'05"0 0111
sw-ou 0"0"'0 011'
.
.
Dissolvec1
Sur race .ater
Metals Sa.pliDg
.esults
Co".r Iron t... UUI'- Mo.nu'- ............ "'rc..r, ...,......-
Ch., .... - CFet. III... c,.t, ..... cu., ..... CMlt, .,... C"'., ..... Cilt., ..... (M8.. .....
../1 .." ../1 .." "/' .." .." ..'I
0.0'. U 0.1 U till till 54.2 0.011 U l1li 0.04 U
0.0'0 U 0.058 0.004 U l1li 48.. 0.0'4 0._' U l1li
.0250 U " .100 U " .0050 U " .0141 " 45.)0 .0J14 " ._2 U V .0100 U "
.0150 U V .100 U " .0010 U " .100 U V '1.80 V .01. V ._, U V .100 U V
VALU( QUALlflEAS, NA. "..."t. ...t r.port.. U . An.',... ..., ...t ..toc'"
J . 'r.....t "'ow ..t.ctl... 'Iwlt . . 'r.....t t.. '."r.'.r, .,....
MIA VAlIMIION QUAlfUAS: (110 v."..Uen "..."".r 'ndtcot.. dU. .... ..0' ..... v."..,..,.
. - "-,.,., 'I.. "0' ..t I - I."..t.. v.,,,.
M . '.'c' .,1'. ...t ,. 8O-11G1 r....
-------
"..\
Di880lved
Surface .at:er
lIet:al8 Sa.pliDg
STA'1'IOII ,.
St.tton O.t. NI...' P.t...S... 5.'.1'11... I"".r ""1-
N-.r '...'.01 (NI). oil... CI[ ). 01.... (Ie). dl... CAI). 01.... Cite). ,It...
../1 .." ..'I .." .."
.--- .-- ----..-
$V-OU 07'12"7 0.04 U .. HR 0.01 U 101
$V-0I4 07'07'" 0.020 U 1.18 0.005 U 0.010 U 101
$W-OU 01'10'" OIlY
$W-0I4 OS/22/.. .0400 U " IV V .0130 V .0100 U V 110
$V-0'4 01/27/.. .0400 U V III . .0050 U V .0100 U " 108 v
$W-0I4 07/"/" OIlY
$W-OU 08/11/" OIlY
$W-OU 0'/20'" OIlY
$W-OU 10/04'" OIlY
$W-0I4 11'0"" OIlY
$W - 014 12/01'" DAY
5"-0" 01/05'50 OIl'
5"-0'4 01/02/50 OIlY
ae8ult:8
Slr.,,1 t- ...111- ft. "....011-
Clr). 01.... ClH. ..... CI.). ..... IV I, .....
..'I ..'I .." .."
1.10 .. .. 0.08 U
1.01 0.100 U .. 0.010 U
1.14 V .0400 U " .100 U " .0100 U V
"17 " .8100 U " .... U V .8100 U V
VALUE QUALifiERS, .. - A..I,.. ... r.~or'.01 U - A..I,..01 .... .., ...,..,...
J - ~r....' ..,.. ...,..'10. '1.1' 1- 'r....' I. I...r.,.r, .,..,
DAIA VALIDAIiON QUAlfiERS, INo .....oI.tlo. 'Iu1lflor 1.00'cot.. d... h.. .0' .... ...1101""'.)
. . """'" tt- .., -, I . htt-'''' ".1...
M . ..,., .",. .., .. 1O-11Ga r....
. . A.J.ct.oI, A - Ac..,'.". ..,. '1...11'1..'1...' V - V.I'"
.
-------
Dissolvect
STATION 64
Stettoft 0.'. line
"""'n 18.,1041 (101). oil...
.."
-- ---- ..----
N-H' 07''1'1''7 0.0'1 U
SV-H. 07/°7/" 0.0'11
N-O" 0"'0'" IMIY
SV-O" 05''l'l'" .0'100 U II
SV-O" HI'I7'" . 01'10 "
N -0" 07' ",.. IMIY
IV-O" 08/"'" l1li,
N-O" 0"'10'" l1li,
SV-O'. 10/0.'" IMI'
N-OU "'0"" l1li,
N-OU 1'1/01'" IMI'
N-OU 01'05"0 OR'
N-O" 0'110'1"0 IMI'
Surfaa. Water
lIetala sa.plinCJ
VAlUI QUAllfIIAS: NIl. Ano',.o .0' ropor.od U . An.',.od ~. .0' .o.oc,..
J . 'r..8nt "'OM ..'eetton .,..t . . 'r...Rt '" 1.~r.'.rr ~I.R'
DATA VALIDATION QUAlfIIA5. (No v.'ldo'lon qu."'lor 'ndleo.o. 410'0 -.. .0' boo. vol'..'''.)
.
aesulta
. . He,.,.. ".. .0' .., I . I."..,.. wo,~
. . 'o'e' .,1.0 no' ,. 8O-IJoa ro..o
. - .0Joe,o., A. Aeeo,'..'o .". .ua""e."o... V. Va".
-------
Surface .ater
oissolve4 Hetals 8..pling Results
8'1'&'1'IOH 103
Stetlon 0.,. Ah-tn... A"U-".. Ar'.fllc lul- ler.."1- Co...1- C.lel- Coot- Chr-t-
"_.r So.,I.d (AI), dho. (U), ""0. (Ao). dl... (I.). ..toO. (Ie). dtoo. (Cd). ..too. (C.). ..to.. (Co). dtoo. (Cr). ..too.
--./1 ../1 --./1 ..'I ../1 ../1 ..'I ..'1 ..'1
-------- -----
5\1.101 0'/"/88 o.on 0.&00 u 0.002 U 0.1'1 0.002 U 0.004 U ".. .. 0.020 U
5\1.101 01'21/1' .200 U V .08CI0 U II .0100 U II .100 U V .0050 U II .0010 U V III ( IU V .0100 U II
5\1.101 05/15'" Doh "0' ..., recet"e"
5\1. 10J 08/15/.. .200 U II .0800 U A .0100 U " .200 V .0050 U II .0050 U A 121 V IU Y .0100 U V
5\1.101 O1/n/.. .200 U V .0800 U A .0100 U A .100 U v .0050 U V .0010 U Y III y IU Y .0100 U v
5W.IOI 01/02/" .200 U A .0800 U V .0100 U V .100 U v .0050 U v .0050 U , III , IU , .0100 U ,
5\1.101 0'/0'/" Oa,a "01 rat rec.tved
5\1.101 10/OJ/" .0100 U II .500 U v .0020 U V .151 v .0020 U v .0040 U v 101 V .0010 U V .0200 U V
5\1.101 11/01/" 0.'. not yet rac.tved
SW.IOI 12'0'/" 0.,. "0' ..., roc. h.d
SW.IOI 01/1./.0 D.,. ..0' ..., roc.lv.d
SW-IOI 02/12/80 0.'. not ...t racet.ed
SW.IOI 01/22/10 D.h "ot ...t rac.tv."
vALUt QUALlfl(IIS: "II - A"'I..t. "ot r.port... U - "..01...... _ut ''0' d.'.ct.d
J . 'r...'" ..10. ..'8ctlon t..lt . . 'r...ftt 1ft ',"rater, .,...
DAIA VAL IDA I ION QUAL FlEAS: (Ho vII'datton qua"ftar Indlcat.. da'l ~.. no, b.,n "."41"..)
. . ""Idt.., U- ''0' -t 1 . lo"-t'" ...Iu.
N - I.tch 0.'" "., t.. to-IIGa r...,.
. . ..J.et.dl ,,- Acc.p'o_l. .tth ~uolt'tc"""ol
v - v.ltd
.
-------
'.
.
Surfaae Water
Dis8olve4 Metals sa.pliDg Results
STATION 103
Statton o.to Cobolt Co"er I,.on Lo.'
II_or 5...10' (Co), .1... (Coo). .1... (fo). .1... ("), .1...
"/' ../. "/' ../.
--------- -- .~--------
$V-IOI 07/11/88 0.0:l0 U 0.0:l0 U 0.061 0.004 U
W.lo' 0./21/.. .01100 U V .0280 U R .111' " .00110 U R
$V-IO' 011/25/" DolO "ot ,ot rec.t"e"
$V-IOI 01/111/.. .0500 U V .0280 U V .100 U V .00110 U V
$V-10' 07/U/.. .01100 U V .0150 U " .100 U V .00110 U "
SV-IO' 01/02/.. .01100 U V .0150 U R .100 U . .0050 U V
S"-IO' 0'/07/" 0.18 "ot ,.t rec.t"e"
S"-IOI 10/01/.. .0200 U V .O:loo U V .0851 A .0020 U V
511-10' 11/01/" 0.,. not ret receIved
SV-IO' 12/01/.. 0.18 ".t ,., r...I"..
SV.IOI 01/18/.0 DolO "0' ,., r.c.l"o'
S"-IOI 02/12/'0 Oa.. not ,., r... ho'
S"-IOI 01/22/.0 Ooto "01 ,at racat"..
VAlOt QUAllfl(RS: HR. A".I,to "ot ro,orto' U . A..ol,.od but .ot ..toct..
~ . 'r...ftt "'ow ..'.ctt.- ,..tt . . 'r...n' t. '."r...r, ~,...
DATA V"lIOATION QUAl'I(AS, (No ".'1'0110" ~uoT"I.r '"dlcoto. do'. ~oo "ot bo... "01"0"'.)
Ltt..,- ........... Mln,...... "'rc..r~ ....,....-
CLI). dI... (Me). .h.. C-). ..... (Me). ..,... (...). ..to..
../1 ...,. ../. ../. ..,.
II. 11.0 0.010 U 0.0002 U III
.0100 U A 12.10 V .01" " .1007 " .0100 U "
.100 U A au V .0150 U . .00011 " .100 U A
.100 U A 12.60 ' .0.1" .0001 U " .100 U "
.100 U V 11.10 ' .06" ' .-1 U . .100 U "
.0110 A 11.70 V .0710 V .0002 U " .500 U V
. - "'1"'.. tI- "ot -t I - Iotl_t.. ".,...
II . 'o'c" .,1'. ".t ,. ID-IIOS r....
. . ..Jo.tO'1 ,,- Acc."o.', .1" ,,,o".'col'o,,o;
-------
Dissolve4
surrace Water
Ketals s..plinCj
Results
STATION 103
St.tton 0.'. Hfchl ..,...f. 50 I.n 1II1II SlIv.r 5.... Stro..tt. ,..11.. tI" v......
H-.r 5...1... (Hf), .1... (I ), ..... (So), df... (A.), ..... CNo), ..... (Sr), ..... In), .h.. Is..), ..... CI ). .h..
../1 ../1 ../1 ../1 ../1 ../1 ../1 ../1 ../1
------- -----
SW-IOJ 07/11/88 0.020 U O..!IJ 0.005 U 0.010 U II.J 0.J'5 O.JOG U .. 0.010 U
SW- 10J OJ/U/., .0400 U A 5U A .0050 U A .0100 U v 11.70 A .420 A .0100 U A .100 U II .0100 U II
$V-IOJ OS/25/.' Ooh ..., ..., recetv."
$V-IOJ "/IS/.' .0400 U " IU II .0050 U V .0100 U A IU V IU II .0400 U " .100 U A .0500 U V
$V -IOJ 07/U/.' .0400 U II SU V .0050 U A .0100 U A 14.10 V IU II .0100 U " .100 U " .0100 U A
$V- 10J 08/02/.' .0400 U V 5U Y .0050 U " .0100 U II 11.10 V IU V .0100 U II .100 U Y .0100 U "
$V-IOJ 01/0'/.' Ooh not ,., rec.t"...
$V-IOJ 10/OJ/.. .0200 U II .147 " .0020 U II .OJOO U II U.JO V .421 V .OOJO U V IU II .0100 U II
$V-IOJ 11/01/.' Ooh not ,., recetved
$V-IOJ 12/"/.' 08'. ..., ,., recetv.'
SW-IOJ 01/18/90 0.,. not ,., recet"ed
SW-IOJ 02/12/90 0.'. not ,., rec.I"."
SW. 10J OJ/22/90 0.'. "01 ,., rac.'".d
VAlUf QUAl.'.fIlS: HII. A...I,I. "01 r.porl.d U. A...I,..d .ul ..1 ..,.c,..
J . 'r...,,' ..1.. d.'.c'lo.. 11.'1 . . Pr....t I. I...r.t.r, .1..'
DATA VALIDAtION QUAL' If AS. (No w.l.d.,I... qu.lf'f.r ...dlc.'.. d.'. h.. ..0' ..... w."d.'...)
. - ........ tt- ..., -t I - 10"-'" v.,,,.
N - I.tc. .,1'. ...t ,. 1O-12Ga r....
II . ..J.CI.dl A. Acc.,I..'. .1'. ...."'lc."o"'1 V - V..,.
'.
-------
STATION 103
St.tton 0.'. ZInc
".-It.r $_'od (I..). ""0.
"/'
-.-----'-- -...-----
W-IOJ 07/11/818 0.014
W-IO' OJ/U/. .0100 U II
$V-IOJ OS/25/. 08to not ...t r.c.tv84
$V-IOJ 01/15/.' .0200 U V
$V - 10. 07/ U/., .0100 U V
$V-10' 08/01/. .0100 U V
W-IO' 0'/07/. 08'0 IIOt ...t reeetv."
$V-1o' 10/0./.' .0270 II
$V-10' 11/0./.' 08t. not ..., r.e.I"."
$V-10' 11/"/.' 08'. II.' ..., roc.I....
$V-10' 01/10/10 08to "0' .... ree.'''..
$V-10' 02/11/'0 Do'. ..0' ..., receive.
$V-10' O./U/IO 08.. no' .... roee I.....
Dissolved
Surface Water
Metals Sa.plinCJ
VIILU( QUIILlfIEAS: NA - A"ol"o no' ropor'od U - II"o',.od byt ..0' ...toc....
J . 'r.'.Rt ~.'ow 4et8ctloft 1'.1' . . 'r...At .. '."rater, .....
DA'" VAL 10111 ION QUIILfIEAS: (No ,,01 Ido' 1o.. quo"'lor I..d'eot.. do'o ~oo .... bo... .0""0'.",)
Resulta
. . ...,...., It.. ..ot .., I - 1."-'" ".1ue
N . O.'c. .,.,. ...t ,. to-llGa r..O.
. - .0Joe..", II - IIee.,.o.'. .1'. qu.II"e.'lono,
-------
-------
.
APPENDIX B-3
SURFACE WATER SAMPUNG RESULTS
TOTAL METALS
S"',"FA::E WATE'" IN'TCRIt.4 ~MEOIAL AC':'lON P\.AN
'"Ceo(" .;.A~S P;.AN':'. i:oOL.OEN. CO..ORADO
'9&; ~'r-= W8,1n"r. .&Q~C.o;l
-------
Surface Water
Total Metals sa.pling ae.ults
903-PAD AND LIP SITB
St.tton Dete Alu.tnu.. A"tl_..y' Ar.8ntc ..rt- '.ryll 1- C...I- C.lel- C..I- Ch....l-
H.....r 5.....1... (AI), totel (SIt). tot.1 (A.). tot. I (I.). tot.1 (I.). t.t.1 (Cd), tot. I (ee), tot.1 (Co). tohl (Cr). t.,.1
../1 ../1 ../1 ../1 ../1 ../1 ../1 ../1 "/'
$V-OSO / / ORY
$V-OSO 01/21/81 I".uftlel.", 5...1. ar lot. I Met.l. A...ly.l. aot roqu..t....
$V-050 M>/21/88 IS.6 .040 U .010 U .4111 .0011 U .005 U 118 NIl .0282
!iV-OSO M>/21/88 I".uffle I."t 5...1. or Tat.1 Met.l. A...lr.l. aot requ..t.d.
$V-OSO 04/81/" DAY
$V.OSO OS/IO/.I ORY
$V-OSO M>/21/.. 1.84 " .0100 U A .0100 U A .J81 " .00so U A .00SO U A 122 A IU " .0148 A
$V-OSO 01/18/81 lI.tO A . M>oo U " .0100 U A .no " .00110 U " . 00110 U " 121 " IU " .01" A
$V-OSO 08/11/81 DAY
!iV-OSO 0'/12/8' DAY
!iV-OSO 10/04/8' DAY
$V-OSO 11/01/81 DAY
$V-OSO 12/01/81 DAY
$V-oso Ol/OS/IO DAY
$V-OSO 02/02/10 ORY
$V-OSO 01/11/10 ORY
$V-OS I 01/21/81 In...ftlel...t 5...,. or Tot.1 Met.,. A""r.l. aat r.q....t.d.
$V-OS I 04/21/88 ORY
$V-OS I 04/81/81 ORY
$V-OSI OS/IO/8I DAY
$V-OSI 06/21/" 2.25 " . 0600 U A .0100 U " .201 " .00SO U " . 00110 U A 104 A IU " .0100 U "
$V-OSI 01/18/" ORY
$V-OS I 08/11/81 ORY
$V-OSI 0./12/81 ORY
$V-OSI 10/04/81 OAY
$V-OSI 11/01/81 ORY
$V-OS I 12/01/11 ORY
$V-OS I Ol/OS/IO DAY
$V-OS I 02/02/10 DAY
SV-OS2 01/21/81 In.uftlet...t 5...10 ar lot.1 Met.l. An.11'" aol roquo.t....
$V-OS2 01/21/88 4.21 .040 U .010 U .2 U .00s U .OOS. U ".2 NIl .010 U
$V-OS2 04/11/81 DAY
$V-OS2 OS/IO/" DAY
$W-OS2 011/0./81 DAY
"ALUI QUALlfIIRS: HI - A...lrt. ..ot roport.. U - A...ly.." but ..ot ..t.et..
J - 'r...nt ..1ow detection ...It . - Pr...n' In '.'.re'err ~1.n'
DAIA VALIDA I ION QUAlfIIA!i: (Na v.lld.tlan qu.II'lor Indle.t.. d.t. h.. "at b..a v.lld.t...)
. - ",1.'.. 'I.. ..at ..t 1 - I.tl..t.. volu.
" - I.teh .,1'. ..0' I. to-11Ga r...o
. - ..J.etodl A - Aecopt.bl. .Ith qu.llfle.tla..., ,,- "oIl'
-------
..
surtac. Water
Total Metals S_plinq R.sults
'03-PAD AltD LIP SITB
Stot Ion o.to Cob. It Coppor Iron L.... Ltthl- ...,....1- MI",."... Horc..r, Ho.,Wo..-
N_or 5..,10" (Co). 'oto I (Coo). toto I (fo). toto' ('b). toto I (Lt). .oto' (...) . toto. (Nn). toto. (H8). toto. (Ho). to.o'
89/' 89/' 89/' ../. ../. 89/' ../. ../. ../.
----- ----- -.---..-.--
$V-050 / / DAY
$V-050 01/2./81 Inaufltc 'o..t 5."'0 or lotol Ho..I. A...I,.,. no' ro.uoa.o...
$V-OliO ./21/88 .0110 U .On8 21.8 .0..4 Nil 13.' .211 .0002 U Nil
$V-OliO ./21/88 In.ufltc '0'" 5..,.. or 10'.' Ho..I. A...".,. not ro"..o..o...
$V-OliO 0'/11/" DAY
$V-OliO 011/10/89 DAY
$V-OliO ./21/" . 01100 U V .0lSO U A .. A .0'7' V ..00 U A 11.10 V ...1 V .0002 V .100 U A
$V-OSO 01/'8/" .0500 U V .0210 U V ".10 II .0111 II .100 U V 12.10 V ."" V .0001 U V .100 U V
$V-OliO 08/1'1/" DAY
$V-OSO 0./12/89 DAY
$V-OSO 10/0./811 DAY
SW-050 11/0)/81 DAY
$V-050 12/01/81 DAY
SW-OIIO 01/011/90 DAY
$V-OliO 02/02/90 DAY
SW-OSO 0)/11/90 DAY
SW-OSI 01/21/81 I.....fltc ,.... 5..,1. or 10..1 Ho..I. A...I,.,. ..0' ro...o.to".
$V-OS I ./U/88 DAY
$V-OS I 0./11/81 DAY
$V-Oil I 05/10/89 DAY
$V-OSI ./21/81 .0500 U V .0250 U V 2 " .00110 U II .100 U II '.11 V .0284 V .0002 U V .100 U II
$V-OS I 01/18/" DAY
$V-OS I 08/11/" DAY
$V-OS I 0'/12/" DAY
$V-OSI 10/04/" DAY
$V-OSI II/OJ/8I DAY
$V-OSI 12/01/" DAY
$V-051 01/05/90 DAY
$V-OSI 02/02/90 DAY
SW-052 01/21/81 I.....fltclo..' 5..,10 Or 101.1 HoI.I. "...1,.1. ..ot r.......ted.
$V-052 ./U/88 .050 U .0lS U ) .0)" "II 1'.5 .0)01 .0002 U "II
$V-OS2 04/11/8. DAY
$V-052 05/10/.. DAY
$V-OS2 Ol/U/" OilY
VALUE QUALlfIEIIS. Nil - IIn.I,I. "0' roporl... U - "...1'.0" b..t "0' "o'octo"
J - Pro....1 1101.. "otoctlo.. II.tt 8 - 'ro.o... I.. I.borator, bla...
oAI" VALIDAIION QUAlfIERS. ("0 v.II"at'o.. "...llf'or I.."lc.to. d.t. h.a ..ot ba... v.lId.'o".)
. . Ho''''''1 tt- Rot ..t I - (.tt_'.4 v.I...
N - aatch 0,1'. ..ot I.. 1O-11Ok ra..,.
-------
'..\
Surfaae Water
Total ..etals Sa.pling ae.ults
'G3-PAD AND LIP SITB
Sutlo.. Ooto Hlc"1 Poto..l.. 5810..1- Sihor Sodl- Stront tw. '''0111- TI.. "....dl-
H-or $o.,Iod (HII. tot.I (It I. totol (Sol. toto I (Atl. toto I (Hel. totol (SrI. to'ol (TI). '.tol ($..). Toto I IV I. ,.t.1
-./1 -./1 -./1 -./1 -./1 -./1 -./1 ../1 ..II
--..--- -..--.--- ...--- - .-....-- -----
$\1-050 / / OIlY
$\1-050 07/21/87 houftlc'o,,' 50...10 or '0'01 Motolo A..olr'" ..ot nquutod.
$\1-050 01/27/18 .0154 5 U .005 U .010 U U .... .010 U HR .0101
$\1-050 01/27/88 Inlufftct.nt S....lo or tot.. ~t." An..,.t. not r...u..ted.
$V-OSO 04/17/8' on
$V-OSO 05/10/8. OIlY
$V-OSO 01/27/8. .0400 U A IIU A .0050 U A .0100 U A 8.14 II IU V .0100 U V .108 A .0500 U II
$V-OSO 07/11/8. .0400 U II IU A .0050 U A .0100 U II 8.85 V IU V .0100 U II .100 U V .0500 U V
$V-OSO 08/11/8. DIY
$V-OSO 09/12/89 DIY
$V-050 10/04/89 DRY
$V-OSO II/OJ/8't DAY
$V-050 12/01/89 OIlY
$V-OSO 01/05/90 DAY
$V-OSO 02/02/90 DAY
$V-OSO OJ/17/90 DRY
$V-OSI 07/21/87 "'"uftlclo..' 5....10 or 'otol Mot.I. A...lro', ..ot roquo,'od.
$\1-051 06/21/88 DRY
$V-OSI 04/17/89 DAY
$V-OSI OS/IO/8't DAY
$\1-051 01/27/89 .0400 U A 5U A .0050 U ,. .0100 U ,. '.40 II IU V .0100 U ,. .100 U ,. .0500 U V
$V-OS I 07/18/89 DIY
$V-OS I 08/11189 DIY
$V-OSI 09/12/89 DAY
$V-OS I 10/04/89 DIY
$V-OS I II/OJ/89 DIY
$V-OS I Il/OI/89 OIlY
$V-OSI 01/05/'0 DIY
$V-OS I 02/02/90 DRY
$V-OU 07/21/81 "'.ufflclont 5....1. or 'ot.I Mot.l. A...lr'" ..ot roquut.d.
$\I-OU 01/21/18 .040 U 5 U .005 U .010 U 4..4 ...0 .100 U HR _050 U
$V-OU 04/17/89 OIlY
$V-OS2 OS/IO/8't DIY
$V-OU 011/09/89 DAY
VALUE QUALlfIEAS: HA - A...lrto ..ot r.port.d U - A...lr..d but ..0' d.toctod
J - Pr..o..' .010. dot.c'lo.. 11.11 . - Pr.....' I.. 1..0r.'orr bl....
DAIA VAIIDAIION QUAlf.EAS: (Ho volld.tlo.. qu.II"or ,..dlc.t.. d.t. ".. "0' bo... volld.tod.)
. . ...,111... tI- "0' _t I[ . htl_toll ..oluo
N - I.'c" .,1'0 "0' I.. eo-IZGa r....o
II . AoJ.ctodl ,.. Accopt.blo ..,,, quollflc.tlo"" V. v.ll11
,
-------
Surface Water
Total Metals saapling Results
'G)-PAD AND LIP SITB
Stet Ion D8t.
HU8bar Sa..lod
-_._~._---
sw-oso / /
SW-OSO 01/21/81
$V-OSO 0./11 /88
$V-OSO 01/21/88
$V-OSO 01/11/8'
$V-OSO OS/10/8'
$V-OSO 06/21/8'
$V-OSO 01/"/89
$V-OSO 08/11/8'
5W-OSO 0'/12/8'
SW-OSO 10/04/8'
$V-OSO II/0J/89
SW-OSO 12/01/8'
$V-OSO Ol/OS/'O
$V-OSO 02/02/'0
SW-OSO OJ/ J1 /'0
SW-OSI 01/21 /81
SW-OSI 06/U/88
$V-OSI 01/11/89
$V-OS I 05/10/89
$V-OSI 0./11 /et
$V-OS I 01/"/8'
$V-051 08/11/8'
$V-051 0./12/89
$V-OS I 10/04/89
$V-OSI ../U/8'
SW-051 12 /0 I /89
$V-OSI 01/05/'0
$V-OSI 02/02/90
$V-OS2 01/21/81
SW-OSZ 01/"/88
$V-OSZ 04/11/89
$V-OSZ OS/IO/89
$V-OSZ 06/01/89
ltnc
(In). toto I
../1
- - --- .-.--
DAY
In'uUlelont 50..10 or '0181 "-18" Anoly'" not requnhd.
.09OZ
In_utllct8nt S...,. or Total M8tat, An.'yt" not requ..tad.
DAY
DAY
.OSO'
.110
DAY
DAY
DAY
DA'
DAY
DA'
DAY
DAY
II
II
'neu'flelo"t
DAY
DAY
DAY
.0200 U A
OIlY
DAY
DAY
DAY
DAY
01"
DAY
DAY
50...10 or '0181 "-18" Anol".. ..ot r84lluo.to".
In,uttlelo"t
.02)1
DAY
DAY
DAY
5....10 or 'otol "-to I, Anoly.l, "ot roquo.tod.
VALUE QUALI'IERS, HR - Anol,t. not roportod U - An.I,..d 'ut "ot dotoctod
J - Pr...nt ~.low de'actlon It.et . - Pra..nt In '..oratory .'8R'
DAIA VALIDA I ION QUAL' lEAS: (Ho vol'''otlon quollflor Indlcoto. d.t. h., not bo." v.ltd.to...)
. . ...I..t.., t 1- not _t I - I.U-h.. ...Iuo
N - 'otch .,1'0 not I.. 8O-IZGa r...,o
. - R.Joctod; A - Ace.pto". .Ith qu.,t'Ie.tton.;
.
V - .,."..
-------
'. ,
Surface Water
Total Metals saapling Results
903-PAD AND LIP SITB
5'."0" De'. Atu.'nura Ant I_n, Ar..nte lorl- lor, Ilt- eo..l- eolcl- C..I- Chr_l-
H""or 58..10" (AI). ,otol (n.. ,0tel (AI). tote I (10). 'otel (10). tote I (Cd), totol (Co), toto 1 (el), to,ol (er). to,ol
..'I ..'I ..'I ..'I ..'I ../1 ..'I ../1 ../1
---- ---.---
SW-05Z 07/07/8' ORY
5101-0112 01/11/11 ORY
$V-05Z 0'/"/" ORY
$V-O!lZ 10/04/" ORY
$V-05Z "/0'/" ORY
$V-05Z 12/01/" ORY
$V-05Z 01/05"0 ORY
$V-05Z OZ/02,.0 ORY
$V-05Z 0'/87"0 OR'
$V-OSS 07/21'87 Inlufttclon' 50....10 or 10tol Hotoll Anol,111 not roquooto'.
5101-055 07/21'87 Inoufttcton' 50..10 or 10tel Hotoll Anol,111 not roquooto'.
$V-O!l!l 01/22'88 .ZO U .040 U .010 U .)10 .005 U .005 U lZ7 l1li .010 U
$V-O!l!l' 04/87'" 6.40 V . 0100 U A .0100 U V .307 V .001' A .00110 U A 101 V IU V .0111 A
$V-O!l!l OS/25'" Dote no' ,ot roco"'od
$V-O!l!l OI,Z',1I 28.JO V .0600 U A .0100 U A .IU V .0050 U A .0050 U A 107 " IU V .0288 A
$V-O!l!l 07/"/" 11.70 " . MOO U V .0100 U " .111 V .00110 U V .0050 U V lit V IU V .0111 A
$V-O!l!l 08/11'" .267 A .0600 U V .0100 U II .JOe V .00110 U V .0050 U " 121 V IU V .0100 U V
$V-O!l!l 0'/20'11 .200 U " . MOO U " .0100 U V .,.1 V .00110 U II .0050 U V IIZ " IU II .0100 U "
$V-OSS 10/11'" .518 V .500 U " .0024 " .ZII V .00ZO U II .0040 U " III V .0010 U V .0Zoo U "
SU-O!l!l ../0./11 .222 .0100 U .0100 U .U5 .0050 U .0050 U 127 IU .0100 U
SU-O!l!l 12/07'" Doto not ,ot recetved
$V-O!l!l 01/""0 Doto not '0' rocolvo"
$V-O!l!l 02/U,'0 Do te not ,ot recelv.d
$V-O!l!l 0'/85"0 Dlte not ,ot receIved
$V-OS7 07/21'87 Inlu'flctont 50...10 or 10tol Hotoll "nol,111 not roquoltO',
$V-OS7 OI,U'88 OR'
$V-OS7 04'87'" OR'
$V-057 05/10'" OR'
$V-057 ../0.'" OR'
$V-057 07'0"" DA'
$V-057 08/11'" ORY
$V-O" 01/"'" OR'
SU-O" 10/04'" DA'
$V-O" II /0"" OR'
VALU[ QUALIFIERS. Nil. ,,"ol,to not roporto. U . Anol,.od 'ut no' 'otocto'
J . 'rolont 'olow 'otoctton 11.lt I . Prooon' In lo'-rotor, .100'
DAIA VALIDAIION QUAlFIER5: (No volldotlon quolt'lor Indtcotol doto hOI no' boon volldoto'.)
. - Holdtnl tt.. no' ..t I . rltt..,o' voluo
M . 'otch l,t.O no' tn IO.IIOS ronlo
. . 'oJoctod; ". Accopto'10 .tt' "ullt'tcottonl; V. Volt.
.
-------
",
,
-
Surface .ater
Total Hetal. sa.pling Re.ult.
903-PAD AHO LIP 81TS
Stet ton 00'0 Cobolt I Copper . Iron L..d lIIlIt- "'."oot- "'"'0"'00 Mercurr ""1,Wo"-
N_or 50"'001 (CD). lote I (CII). 10101 (h). loto' ('11). tote I (lI). tohl (HI). 10181 (...). t.h. (Nt). toto' (Mo). tot..
.,/. ../. ..II ..'I .,/1 ..II .,1' ..I' ..I'
------ --
SW-OIl2 07/07/89 DAY
$V-OU 08/11/8. DAY
$V-on 0"28/8' DAY
SV-OU 10/04/89 DAY
$V-OS2 II/OJ/8. DAY
SV-OS2 11/01/81 DAY
SV-OS2 Ol/OS/.O DAY
$V-OS2 02/02/.0 DAY
$V-OU OJ/I7/.0 DAY
$V-05S 01/21/81 I"sufflcto"' 50.,10 Dr '0101 ...10'0 A"o',s'o "01 r.,.....'ed.
$V-05S 01/21/.1 Ineu"tet.nt 50.,10 Dr '010' ...10'0 A"o',lto "01 r......'.cI.
$V-OSS 06/22/88 .05 U .025 U ..02 .0011 U
$V-OSS 04/17/8. .0SOO U V .02lS " 6.20 V .01SII Y
$W-05!l 05/25/81 0.1. not ret recetv.d
SV-05!l 06/28/8. .0500 U V .OS70 Y 26.70 " .0S76 Y
$V-OilS 07/11/81 .0500 U V .0212 Y n.lo " .OIU "
$V-05!l 08/16/8' . 0500 U V .0250 U " .18' " .00.0 U "
$V-OSS 0./20/81 .0Soo U V .0250 U Y .187 " . 0050 U "
$V-05!l IOfl./8. .0200 U Y .0200 U " ."4 Y .0045 "
$V-OSS 11/°'/8' .0500 U .0250 U .264 .0050 U
$V-OSII 11/07/8. 0018 "01 ,.1 receIved
$W-05S 01/16/.0 Doh "01 "01 rece'v.d
$W-OSS 02/U/'0 0010 "01 '01 received
$V-OSS O./IS/.O 0010 "01 ,.1 rece'v.d
$V-057 07/11/87 l"oufftcto"I 5.""8 or '0181...1810 A"ol,o" "at r~II.lh".
$W - 057 06/U/88 DAY
$W-OS7 04/17/" DAY
$W-OS7 011/10/" ORY
$W-OS7 06/0./8. DAY
$W-OS7 07/07/8. DAY
$W-057 08/11/" ORY
$W-OS7 0"16/8' DAY
$V-OS7 10/04/8' DAY
$W-OS1 11/03/8. DAY
NR 26.'
.08)1 " 21.10 Y
.104 " 26.40 Y
.172 Y '1.10 Y
.1'0 " 11.10 Y
.U2 " 21.10 Y
'.20 " 14.10 Y
...5 21.50
.2011 .OOOJ U NR
...4 Y .0001 " .0275 "
:771 Y .0002 U V .100 U "
..114 Y .OOOJ U Y .100 U Y
.HI Y .0001 U Y .100 U Y
.217 " .0001 Y .100 U "
.280 Y .0001 U " .IlOO U "
.210 .0001 .100 U
VALUf QUALlflfRS: NR. ""01,10 "01 roporlod U . ""ol"od b,,1 "01 dolocto"
J . Pr..."' ~.1OM ..t.ctton ".It . . Pr...n' 1ft '...r.'.rr 'taR'
DA'A VALIDAIION QUAlfURS: (No voltdol1o" q".llftor t"dtcol.. dol. II.. "01 II.... voltd.hd.)
. . No''''o, It.. "01 ..I I . f.t...t... va'".
N - ..tcll 0".0 not t.. 8O-12~ ro..,o
-------
Surfac. Water
Total Metals saapling R.sults
903-PAD AND LIP SITB
Station O.t. H'dol Pot..o,,,. S.'.nt"", Stiver Sodl- Stronll- 'hol1l- tin Vo..04ll1-
NW8ber So...lod (HI). 00001 (I[ ). tot.' (So). toto I (A,). toto I (Ho). 10101 (Sr). totol (n). totol (Sn). 'otol (V). totol
rag/I ../1 .,/1 rag/I "/' ../1 "/' "/' "/'
-------- -.--- ---- --
$\I-OU 07/07/89 OIlY
$\1-052 08/11/8. OIlY
$\1-052 0'/28/" DAY
$\1-052 10/04/89 DAY
$\1-052 11/01/8. DAY
$\1-052 U/OI/.' DAY
$\1-052 01/05/'10 DAY
$\I-OU 02/02/'10 DAY
$\I-OU 01/11/'10 DAy
$\1-055 07/21/87 Inouftlc'ont 50...10 or 'otol Mo.olo Anol,o'o not r841u..ted.
$\I-on 07/21/87 Inoufflctont $0"'0 or lotol Motolo Ano"olo ..ot ro...ootod.
SWoon 06/22/88 _040 U 5 U .0075 .010 U 71.' .87' .100 U HA .050 U
$\1-055 04/17/.. .0400 U A 5U " .0050 U A .0100 U V 42.. V IU A .0100 U V .100 U V .0IlOO U V
$\1-055 OS/25/" 0..0 not rot rec.lved
$\1-055 0./28/8. .0000 U A 7.2' A .0050 U A .0100 U A 31.'0 V IU V .0100 U A .141 A .0852 V
$\1-055 07/1./.. .0400 U V '.U V .0050 U . .0100 U " ".10 V IU " .0100 U . .100 U V .0IlOO U "
$\1-055 08/16/.. .0400 U V 5U A .0050 U " .0100 U " 17.20 " IU V .100 U . .100 U " .0500 U .
$\1.055 0./20/.. .0400 U A tIU A .0050 U A .0100 U " ".10 " IU . .0400 U " .100 U " .0500 U "
SW-055 10/11/.' .0200 U A 2.11 A .0020 U " .0100 U . 61.40 " .112 " .0010 U " IU " .0100 U "
$\1-055 "/0./.. .0400 U 5U .0050 U .0100 U 74.20 lU . 0200 U .100 U .0500 U
$\1-055 U /07 /.. Ooto not ,ot receIved
$\1-055 01/16/'10 Ooto not rot receIved
$\1-055 02/21/'10 Doto not ,ot received
SW-055 01/15/10 Doto not rot rocohod
SW-057 07/21/87 In.uflle'.nt So...lo or lotol Motolo Anolrolo ..ot ro...ooto'.
$\1-057 06/21/.. DAY
$\1-051 04/11/.. DAY
SW-057 05/10/.9 DAY
$\1-057 0./0./.9 OIlY
SW-057 07/07/.. OAY
SW-057 08/11/.9 DAY
$\1-057 09/16/.9 DAY
SW-057 10/04/.9 DAY
$\1-057 II/OJ/.9 OIlY
VAlUf QUAllflfRS: HA - Anol,to not roportod U - Anol,.od but not 'otocto'
J - 'r...nt ~.'ow detect ton I'.lt . . Pr...nt 1ft '.~or.t.r, ~1.ft'
DATA VALIDATION QUAlflfAS: (Ho ..olldoolon quollflor Indlcotoo doto hoo not boon ..olldoto'.)
. - Moldl.., 11- not _t f - (oll_to4ll ..0,..0
H - lotch opl.o not In 1O-12~ ron,o
. - AoJoctod, A - Accoptob'o with ...o'lflcotlono. V - Vol"
;
-------
'03-PAD AND LIP SITB
5tet Ion o.te
N_o,. 5."",lod
-..-----
$\1- 052 07/07/89
$\1-052 08/11/.9
$\1-052 0./2./..
N-052 10/04/.'
511-052 II/OJ/.'
N-052 U/OI/.'
N-052 01/05/90
N-052 02/02/90
N-052 01/17/90
N-055 07/21/87
$\1-055 07/ZI/.7
N-055 06/22/88
511-055 04/17/.9
511-055 OS/25/8.
N-055 06/2./.'
N-055 07/1./.,
511-055 08/18/.'
N-05s 0./20/81
N-055 10/1'/.'
N-055 11/0'/.'
N-055 U/07/8I
N-05s 01/18/90
N-05s 02/21/90
N-05s 01/15/90
511-057 07/ZI/87
$\1-057 M/U/.
N-057 04/17/.'
N-057 05/10/81
511-05' 08/09/.,
N-057 07/07/.'
511-057 08/11/.'
N-057 0,/18/.,
N-057 10/04/.'
N-057 11/01/8'
line
(In). totel
",,/1
-- -_.~----
OIlY
OIlY
OIlY
OIlY
OIlY
OIlY
ORY
OIlY
OIlY
In...'flclo"t
I"...fftcto"t
.141
2.10
v
".
Surface Water
Total Metala saapling Results
5."",10 0" lot.1 Metol. Anoly.t. not ,..~....tod.
5."",10 or lot.1 Met.l. A"oly.t. not r.~..o.t..-
Oat. not reI rec.tved
2..4
1.11
.944
.171
1.01
1.12
o.te "ot yot
o.h no' yot
O.te not yot
0... not yot
V
A
V
A
A
racelvad
racet"...
racelvad
rac.lved
In.ul"etant S.~I. or rot., ~t.,. Ana'r'" not r.~y..t...
DAY
DAY
DAY
DAY
DAY
DAY
DAY
DAY
DAY
VALUE QUAllfl[A5: NA - A".lrto "ot roportod U - An.lr.od b..t "0' dot octo.
J - 'r...nt ..1ow datlctlon ....t . . Pr..,n' In 1.~or.t.r, "ank
DAIA VALIDATION QUAlflfA5: (No y.lldotto" ~...II'tor t,,"c.to. 'ot. h.o not boon y.II..to..)
. . Ho''''.., t t- not .., ( - (I' ,..,.d val".
" . 'otch a,l.o not t" 8O-12~ ra",o
A. 'aJocto.; A. Accoptablo .Itb ~...""catlon.;
.
.,.
-------
. ,
Total
8urface .ater
Metals 8a.pling
Results
'03-PAD AND LIP 8ITB
Slot Ion Dot 0 A1umtnuI8I Antt-nr Ar..ntc larl- 10rrllt- Co.t- Colct- Coot- Cllr.t-
N..der 50...10. (A'), toto' (U), toto' (A8), toto' (10), toto' (10). toto' (Cd), totol (Co), toto' (C8), toto' (Cr). 'oto'
"'9/' ../, "/' "/' "/' "/' "/' ../, ../,
--- ----
$V-on 12/01/8' OIlY
$V-017 01/01/10 OIlY
$V-017 02/02/10 OIlY
$V-057 01/17/10 DRY
511-051 07/21/87 h...ffl.tont 5_'0 or 10to1 Motol. Anolr.l. not roq..o.to..
$V-OM O./U/88 .41' .040 V .010 V .114 .001 V .005 V III NR .010 V
$V-051 04/17/8' DAY
511-051 Ol/IO/~' ORY
511-058 0./28/89 .550 " .0600 V " .0100 V A .212 " .0050 U II .0050 U " 97.10 V .100 V V .0100 V "
511-058 07/14/89 DRY
511-058 01/11/89 OIlY
511-051 0./20/89 ORY
511-051 10/04/89 OIlY
511-058 11/20/89 DAY
511-011 12/01/89 DRY
511-0M 01/01/10 OIlY
511-0M 02/02/tO OIlY
511-017 06/22/88 .0002 V .00004 V .00001 V .000) .005 U .005 U .101 NIl .00001 U
$V-077 01/10/11 OIlY
$V-077 01/11/8. OIlY
511-077 OS/27/89 1.17 " . 0600 V A .0100 V A .214 II .0050 V A .0050 U II II'" Y .100 U II .0100 U II
$V-077 07/18/89 OilY
511-077 08/11/89 2.17 " . 0600 V V .0100 V II .200 U V .0050 V V . 0050 U A 71.)0 V IV V .0100 V "
511-077 09/20/89 DAY
511-017 10/04/89 0111
$V-077 11/0'/11 OA1
511-077 11/01/89 0111
511-077 01/05/tO 0111
511- 077 02/02/tO DAY
511-017 OI/Ii/tO 0018 not rot roco'..o.
VIILVI QUALI'IIA5, NR. Ano'rto not roporto. V - IIn.'r'o. but not dotoctod
J . Pro.ont bo'ow dotoctlon It.lt I - Pro.ont In 'o~rotorr "'onll
DA'A "AlIDA'ION QUAL',IA5: (No y.I'd.tlon q...'tftor In.lc.to. doto h.. not b.on yolld.to..)
. - He'.'.1 tt.. not ..t [ - 18tl..t.. ..0'..0
N - lotc" .p"o not tn eo-lIDS ro.,o
II - lIoJoclod; A. Accopt.II'o .It" ...olt'I..tto.., V. Volt.
-------
4
..
Surface Water
Total Netals Sa.pling Results
903-PAD AHD LIP SITB
Statton o.t. Cobon Coppor Iron l.od llthl- MaI"..'t8I ...".."... Mercur, Mo"......-
""M.r So.., lod (Co). tDtol (eu). toto I (h). tote1 (.b). toto' (lI). toto' (lie). toto' (""). toto, (lie). Iota' (Mo). '0'"
-./1 -.1' ..I' ..I' ..II ..I' ..I' ..I' ..I'
---- ---
5\1-057 12/01/89 DAY
5\1-057 01/°5/.0 DAY
5\1-057 02/02/.0 DAY
5\1-057 03/17/.0 DAY
5\1-058 07/21/87 I..oufflclo..t S...,'o or loto' Mohto ""01'1" ..ot r~u.lhd.
"'-058 "/U/M .050 U .025 U .489 .001 U l1li 20.1 .11 .0001 U HI
5\1-058 04/17/8. DAY
5\1-058 05/10/89 DAY
5\1-058 "/2818' .0500 U V .0321 II .842 V .0050 U V .100 U V 11.30 V . 0457 V .0002 U V .100 U V
5\1-058 01/14/89 DA'
5\1-058 08/11/89 DA'
5\1-058 0"20/89 DA'
5\1-058 10/04/8. DAY
5\1-058 11/20189 DAY
5\1-058 12/01/89 DA'
5\1-058 01/05/90 DA'
5\1-058 02/02/90 DA'
5\1-017 06/22/88 .00005 U .0000:1 U .0001 U .001 U MA .022' .0011 . .0002 U HI
"'-017 0:1/:10/8. DAY
5\1-017 05/1118. DA'
5\1-077 "/27/89 .0500 U V .0250 U V 2.54 II .OUI It .100 U V 24.10 V .404 II .0001 U II .100 U V
5\1-071 01/18/8. DAY
5\1-011 08/11189 .0500 U V .0250 U It 2.12 II .0060 U It .100 U V 14 V .211 II .0002 U II .100 U V
5\1-017 0"20/89 DAY
5\1-011 10/04/" DAY
5\1-017 11/0918. DAY
5\1-017 12/01/89 DA'
5\1-017 01/05/.0 DA'
5\1-017 02/02/.0 DA'
5\1-017 0:1/11110 Dltl not yet recelyed
VALUE QUALifiERS: HR. A,,"I,to ..ot roport.d U - An~I,.od but not dotlctod
J . Pr..."t ~.low 4.tectton 1t.'t . . 'r..."t 1ft '.~r.t.rr ~1.,,'
DAIA VALIDA I ION QUAlfIERS: (No villdltlo" quo'lfl.r Indlcotol doto hOI not boo.. volldat.',)
. . ...Idl... tl.. ..ot ..t 1 . 10tl..t84 valua
H . 'otch 0,1.. ...t I" 80-11«1 ro...o
-------
8urface Water
Total Metals 8a.pling Results
903-PAD AND LIP 81TB
St.tton o.to Hlc"l Poto.. t'" S.'.nlu. Silver so..t- Stront tU8 '''ont- 'h. Vo..o..t-
N.-ber hooplo" (Ht). totol (I( ). totol (50). toto I (A.). toto I (110). totol (Sr). totol (n). toto I (s..), 'otol (V t. toto I
"'9/1 ../1 ..II ..II ..II ..II ../1 ../1 ../1
-.----.- ------
$V-057 12/°1/89 OIlY
$V-057 01/05/" OIlY
$V-057 02/02/.0 OIlY
$V-057 U/17/.0 OIlY
$V-058 07/21/87 In.yUtcto..t S....lo or 'otol Motol. A..ol,.t. ..ot roll-.tod.
$V-OH OI/U/88 .040 V 5 V .005 U .010 V 11.7 .71& .010 V .. .0110 V
$V-OH 04/17/8. OIlY
51/-058 05/10/.' OIlY
$V-058 01/2./.. .0400 V V 5U A .0050 V A .0100 V V ..51 V .41. V .0100 V A .100 V V .0500 V V
51/-051 07/14/89 OIly
$V-OS8 08/11189 OIlY
$V.051 09/2°/" OIlY
$V-051 10/04/.' OIlY
$V-051 11/20/.. OIlY
$V-058 12/01/.' OIlY
$V-05' 01/°5/.0 OIlY
SI/-058 02/02/.0 OIlY
$V-OH 01/22/88 .00004 U .0050 V .005 U .00001 V .0582 .0001 .00001 V .. .00005 V
$V-077 OlfJO/.' OIlY
$V-077 05/11/.9 OIlY
$V-07 7 01/27/8' .0400 V V 5U A .0126 V .0100 U A 44.10 V .101 A .0100 U A .100 V V .0500 V V
$V.077 07/1./8. OIlY
$V-O" 0"11/8' .0400 V V 8.77 V .0050 U V .0100 V A 24.50 A IV V .0100 V A .100 V V .0500 V A
$V.OH 09/20/8. OIlY
$V-OH 10/04/89 OIlY
51/-077 11/09/89 OIlY
$V-077 12/01/89 OIlY
$V.077 01/°5/90 OIlY
51/.077 02/02/90 OIlY
$V-OH 01/16/90 O.t. not ,et recetved
VALUE QUALlfIEA5: HA. A..olrto ..ot roporto" V . A..ot,.o.. but not ..otocto"
J. Pr..."' ~.1~ detect ton It.ft . . Pr.'.ftt In '."rater, _'8ft.
OAIA VALIDA liON QUAlfIEA5: (Ho volt"otton quolt,tor Indlcoto. doto "0. ..ot boon volt..oto".)
. - ...,...., t,- ..0' _t I - (ett-'.. val".
N . 'otclt .,t.o ..ot I.. 80-1101 ro..,o
A . AoJoctO"1 A. Acco,to"10 .Itlt quolt'lcotton.; V. Volt..
.
-------
Total
surface Water
Metals S88pliDg
'03-PAD AND LIP SITB
Stet.on De'.
NY8bor So~lod
$V-OS7
$V-OS7
$V.OS7
$V-OS7
SV-OS8
$V-OM
$V-OM
$V-0!18
$V-OS8
$V-OS8
$V-OS8
$V-058
$V-058
$V-058
$V-OM
$V-OM
$V-OM
$V-OH
$W-OH
$V-OH
$V-077
$V-077
$V-OH
$V-OH
$V-OH
$V-OH
$V-OH
$V-077
$V-OH
$V-OH
--.-..--
12/01/8'
OI/OS/tO
02/02/.0
OJ/17/.0
07/21/87
OI/U/88
0./17/11
05/10/11
0I/l8/"
07/1./8.
08/11/11
0./20/8.
10/0./8.
11/20/11
12/01/8.
OI/OS/tO
02/02/tO
06/22/88
OJ/)O/..
OS/II/8'
01/27/11
07/18/81
08/18/11
0./20/81
10/0./81
11/01/81
12/01/8.
OI/OS/tO
Ol/02/tO
OJ/II/tO
linc
(lrt). total
../1
----
DAY
DAY
DAY
DAY
In...fltctont
.020 U
DAY
DAY
.0544
DAY
DAY
DAY
DAY
DAY
DAY
DAY
DAY
S.~lo or 'otol Hotol. Anol,.t. not roq..o.tod.
A
.0000J
DAY
DAY
.lIe
DAY
.052.
DAY
DAY
DA'
DAY
DAY
DAY
D.'. not ret received
'i
A
VALUE QUALlfl£RS: NA. Anol,to not roporto. U . Anol,.od but not dotoctod
J . Pro.ont below .otoctlon 11.lt , . Prooont In loborotor, blont
OAIA VALIDAIION QUALfl£AS: (No voll.otlon quollflor Indlcoto. dot. h.. not boon .olldoto..)
o
..
Results
. . Hold tn. tt- not _t [ . [o"_t04 0101...
N . 'otch o,lto not In 8O.IZGa ron,o
-------
--,
Surface Water
Total Metals s.-pling Results
STATION 53
Stot Ion o.t. AI_ln- Ant I_n, . Are.nte lorl- lor"11- C...I- Co'cl- Co.I- C"r_I-
1I_.r So.p lod (AI), toto I (5b), tot.1 (A.), toto I (I.), tote' (10), tote I (Cd), tote' (Co), toto' (CI), tote' (Cr), toto'
..,/1 ..I' ../1 ..I' ..I' ..I' ..I' ..II ..II
---- ------ -------
!W-OII 01/21/.7 In.uUlc lont So.." or lot., Hot.,. Anl',111 not ro,uolte".
!W-OU M/U'" 2.11 .060 U .010 U .'It .001 U . OO!I U 111 NIl .010 U
$V-OIl M/U'" In.uUlclont 5''''0 or lotol Met.'e An.lr_t. not r..uo.t.d.
$V-OU 0./01/.. NIl HI HA HI HA NIl NIl HA HA
$V-OU 01'21'" ..11 V .0600 U A .0100 U A .216 V .0010 U V .0050 U A II' A IU V .0100 U A
$V-OIl 06/2.'" '.'2 V .Moo U V .0200 U V ..48 V .0011 V . 0050 U A II. V .100 U V .0100 U V
$V-OIl 07' ",.. DAY
$V-051 0'/11'" .200 U A .0600 U II .0100 U A .212 V .0010 U V .0050 U " 160 V IU V .0100 U V
$V-OIl 0'/20'" .200 U II .0600 U A .0100 U V .266 V .00110 U . . 0050 U V 142 " IU . .0100 U "
$V-OIl 10/12'" .600 " . 0600 U V .0100 U A .211 V .0010 U V .0050 U V II. V 2.110 U V .0100 U V
$V-OIl 11/01'" o.to not ,e' ree.tva.
$V-OIl 12/11'81 Oot. not '01 raeetvelll
$V-OIl 01/11'90 001. not ,ot recetved
$V-OIl 02/""0 Oote not ,ot reeetved
VALUE QUAllfIEAS: NIl. Anl"to not roported U - An",.od bul not ...toctod
J - 'ro..nt "low "otoctlon 'I.lt . . Pro..nt In ','.r.tor, b'...
OA'A VAlIOA'ION QUAlfl(AS, (Ho vo'ldltlon qu.llflor Indlc.to. d.t. h.. not boon v.'I"ltod.)
. . ...1..1., tI- .ot -t ( . htl_t... v.'ue
H . I.tc" 1,1'. not I. 8Q-I'lGa r...o
I . A'J.ct.dl A - Accopt.b'. .It.. .uI'Iflc.tlon.,
V . V.II..
o
-------
0;
Ii
Total
surface Water
Metals sa.pling
.esults
STATION 53
St.tton D... Co'"It C......,r Iron l.... l It lit. Ma.n..'. "'".on... Harc..r, "",wo".
H-.r "...1... cc.). 'otol cc..). '0'.1 CFe). '0,.1 c,..). ,.to' CLt). '0'01 CMe). 'ohl CMII). '.hl CHt). ,.to' Clio). '.tol
../1 "/' "/' .." .." "/' .." "/' "/'
---- ---
$V-on 07/2'/'7 '",,,'''c ,..., 5...110 or Toto' ""01. A".,y.,. "ot r......."".
$V-on 01/21/.. .050 U .015 U 1.15 .0111 NIl II .712 .0002 U HI
$V-OSI 01/21/.. ,,,...ltlcl.,,' S....,. or Toto' Ho'olo Anoly.l. "ot ro"..o."".
$V-OSl 04/05/81 HI HI l1li .0050 U "I NIl NIl IIA NIl
swoon OS/21/11 .0500 U A .0250 U A '.12 A .0050 U A .0240 A 2'.'0 " .111 A .0002 U V .0100 U "
swoon 0./26/81 .0500 U V .01" " 22.10 V .0200 U V .100 U V 11.10 V .71' V .0002 U V .100 U V
SW-OSI 07/1./81 0111
5W-OSI 0"111'" .0500 U V .0250 U " 5.'4 V .0010 U " .100 U V 27.20 V .1101 V .0002 U V .100 U V
sw.on 0./20/81 .0500 U V .02!l0 U V 5.0' V .0050 U V .100 U I 14.'0 V ..,4 A .0007 V .100 U A
5W.OS' 10/11/11 .0500 U V .0250 U " 1.47 V .0010 U I .100 U V 28.20 V .4" A .0002 U V .100 U V
SW-OSI 11/07/.. 0.,. "ot 18' recetved
5W.OS. II/IS'" O.to "., Y.' received
$V-OSI 01/17/10 0"0 no' yo. received
SW.OSJ 02/U/.0 o. to no' y.' received
VALUf QUAL'flfAS: "A. "n.ly" no' r.por'." U . Anol,..d b.., no' d.'.ctod
J . Pro.on' ".'011 ".'.c"on I'." . . 'r...nt 'n '...or.tor, "10".
OA'A VALIOA'ION QUALflfAS: (Ho ...lldo"on q...'I'lor Indlco'., do'o ho. no' boon ..."doto".)
. - Holdl", 11- no' -, [ . [.II_to" "0'''.
" . '.'ch 0".. n.t ,,, eo-11Ga ro...
. - ..J.ctod. A. Acc.p'o"'. with "",""co.lonl,
-------
8urfaae Water
Total .etals 8a.pling R.sults
8TATION 53
Statton o.t. Hlch' Pot... t.... $.'."11- Stlvor SocII - St ro..t ,... lhe'lI- It.. "0"0.'-
HU8b.r So",'od (HI). tout (I ). tout (58). toto' (A,), to18' (He). toto' (Sr). to18' cn). toto I (s..), loto' C., ). toto'
-'/' "/' ../1 "/' ../1 ../1 ../1 ../1 ..'I
-....----- --------- -- -.----- .----
swoon 07/2./87 'nluff'etont s_to or loto' Hoto'" Ano"Otl not roqu..18..
sw-on "/21/88 .040 U 5 U .OOS U .010 U 17.' .802 .010 U HA .oao U
sw -on 0./21/88 'nlufflelont S_'o or 1018' HotO'" Ano,,"11 not r.......ted.
SW-OSJ 04/05/8' ItA ItA HA HA ItA HA NIl HA IIA
swoon 05/U/.. .0400 U A au A .02S0 U A .0100 U A 20.10 V IU V .0100 U . .100 U II .0!lOO U A
swoon "/21/" .0400 U V au II .0050 U A .0100 U V 17.10 V .847 V .0100 U I .IOt V .0!lOO U V
SW-O!IJ 07/1./.. DRY
sw-on H/15/8' .0400 U V 5U V .ooso U ., .0100 U A 14.70 IU V .100 U I .100 U ., .OSOO U A
sw-on 0./20/.. .0400 U A au A .0050 U I .0100 U II ".10 A IU . .0100 U II .100 U II .0!lOO U A
SW-OSJ 10/12/8' .0400 U V au R .ooso U A .0100 U V 1..40 V .716 A .0100 U A .100 U V .0500 U V
SW-OSJ 11/07/.. Do.. ..ot ,ot race' ",ed
5W-OSJ 12/IS/8I Doh not ,ot rec.lved
$W-OSJ 01/"/'0 Doh not ,ot r.cotved
$W-OSJ 02/U/.0 0018 not ,ot rece.wed
VAlU[ QUAllfl[IS, ItA - A..o.,to ..ot ro,ortod U - A""'"o. ~ut not .otoct...
~ - 'r...nt bel.. 4e'actton It..t . . Pro..ftt In ',"ro'or, .'8W'
DAIA VALIDA liON QUALfl[AS: (Ho vo'l.otto.. quo'tftor tndlcotol dote hoo not boon vo..doto..)
. - Ho'.'''' ,t.. "0' .., I - [o,t..,o. woluo
N - 'o'ch 0"'0 no' ... 1O-1~ ro..,o
R - 10Joc,0.1 A - Acco,'"~10 .t,~ quoltf'co't.""1
., - Voll.
..
-------
Surface Water
Total Metals saaplinq Results
STATION 53
Statton Oat. ltnc
"..-bar 58...'od (In), totel
../1
-------
SW-OU 07/21/87 InluUlclont
swoon O6/U/88 .0252
swoon O6/U/88 Inl..fflctont
SW-Ou 04/05/" IIA
sw-ou OS/2J/" . 0200 U R
SW-05) 06/26/.. .121 V
SW-05J 07/11/89 OAY
SW-05) 08/15/" .0200 U R
sw-ou 0'/20/" .02" "
sw-ou 10/12/" .0288 "
sw-ou 11/07/89 Deh not 110' recolved
SW-OU 12/15/89 01'0 not lIot rec.'ve.
SW.OU 01/17/'0 Do" not lIot r'.c. t 'led
SW-O!iJ 02/1J/'O On I not lilt rece'ved
So...I. or 10..1 He.... "nlllll" not ;.equol..d.
S8"" or tot., ~t.l. An.lrl" not requ..'ed.
VALUf QUALlflfRS: HI. Anlillto no' roportld U . Anlillood but not .0toct04
J . 'r..,nt below detoctlon I..lt I - Pr...nt In '.~.r.t.r. .'Ift'
DATA VAllDAIION QUAlflfAS: ("0 volldotlon qUII'f'or 'ndlcoto. dltl ~Ol not boon vIII.o'o..)
. - NoI.I.. tI- no' -t ( - (ItI..to. vol,,"
M - 'otc~ 1,lt. ftot I. IO-I~ rl".
. - .0Joctodl A. Acco,tlblo .Ith qUII'f'clt'onl,
..
v - VI".
-------
Surface Water
Total Metals s_pling Results
SOUTH WALHUT CRBBK
Statton Doto AI_In- Antl-n)', Arunlc 'ul.. "r)'l1t.. Co.," C8le'.. Cn'.. CII....t..
H_or 50"'0" CAI). total cn), total CA.). total C'o), total C'o), total CU), total (Co), toto I (C.), total CCr), tot. I
../1 ../1 ../1 ../1 ../1 ../1 ../1 ../1 "/'
----- -----
5\1-05' 07/21/'7 In.uUlclo..t 5_'=- or lotol Motol. Anol)'.I. not ro"uo.to".
$V-O" 0./310/18 5.31 0.060 U 0.010 U 0.3 0.005 U 0.005 U no HII 0.010 U
$V-0511 04/U/... 25.40 V . oaoo U A .0100 U A .244 V .0111 A .0010 U A U V IU V .0'" V
$V-05' OS/II/" 11.10 v . oaoo U v .0100 U A ..4 V .0050 U A .0050 U . 1111 V IU V .0141 A
$V-O" 0./07/.. .3104 A .0600 U A .0100 U A .ltJ A .00110 U A .0050 U V nil A .100 U V .0100 U V
$V-0511 07/12/'8 ..18 V .0600 U V .0100 U V .144 V .0050 U v .00110 U A no A IU . .0100 U V
$V-os. 01/0'/" 4.40 A .oeoo U A .0100 U A .1" V .0050 U II .0050 U V 12' V IU V .0100 U I
SW.OSII 08/14/.. .11317 v .0600 U A .0100 U V .101 V .0050 U A .0050 U II loa A IU A .0100 U I
SW-OSI 10/1'/" Oota not ,ot r.c.tv.d
$V-on 11/15/" Dota ..ot ,ot receive'
SW-0511 12/1'/" Dota not ,ot race t vad
SW.OSII 01/25/.0 Ooto not ,ot recetved
SW-0511 02/22/'0 0.'. not ret r'.cetvad
$V-OS' 01/21/'0 Ooto not ,ot recetved
SW-060 07/21/87 In.uUlelont So"",lo or Iota I Motol. Anol,.,. not r.,.....to".
5\1-0110 11/11/" In.uUletont 5_10 or 'otol Motolo Anol,... not r.,....o tOIl.
SW-OIIO 07/01/.. 0.200 U 0.060 U 0.010 U 0.200 U 0.005 U 0.005 U 108 HI 0.010 U
SW-060 01/../.. .100 U A .oeoo U A .0100 U A .100 U A .0010 U " .0010 U . 10.10 V IU V .0100 U I
SW-060 OJ/I./.. .200 U . .0600 U . .0100 U " .200 U A .0050 U " .0050 U V 81.20 V IU V .0100 U A
SW-060 05/111/.. .200 U I .0600 U V .0100 U V .200 U V .0050 U " .0050 U . 71.20 V IU V .0100 U V
SW-OIIO 05/15/.. .200 U A .0600 U V .0100 U V .200 U V .0050 U " .0050 U . 70.20 V IU V .0100 U V
SW-060 oa/O'/" .2.2 A .0611 " .0100 U Y .200 U " .0050 U " .0050 U . .4 A IU V .0100 U A
SW-060 07/06/.. .... V .0600 U V .0100 U " .111 V .00so U V .0050 U V 110 V IU V .0100 U V
SW-OIIO 01/01/.. .2" V .0600 U II .0100 U V .100 U V .0050 U II .0050 U V 101 V IU V .0100 U V
$V-OliO 08/11/.. Dota not ,ot race t vad
SW-OIIO 01/11/" Doto not ,ot roco ho"
SW-OIIO 10/01/" .0100 U A .!IOG U V .0020 U V .17' V .0020 U V .0040 U V t5 V .0010 U V .0100 U V
SW-OIIO 11/06/" 0.'8 "ot ,.. recetved
SW-OIIO 11/06/.. Doh not ,ot roco'vo"
SW-060 U/08/.. Ooto not ,ot rec.lva..
SW-OIIO 01/21/80 O.ta not ,ot recelv.d
SW-060 02/0'/80 Data not ,ot recelvad
SW-OIIO 01/12/10 Oa'a not ,ot recelv.d
SW-061 07/22/., In.utllet.nt Sarap1. or lotol Motol. An.I,.I. not roquo.to".
VALUE QUALI'IEAS: NA - Anol,to not roportod U - Anol,.o" but not "otoetod
J - 'ro.ont .olow dotoetlon 11.lt . - 'ro.ont In 10borotor, blon.
OAIA VALIOAIION OUAl'IEAS: (No volldotlon q.oll'lor Indleoto. doto h.. not boon voll"otod.)
. - Holdtn, tt.. not ..t « . [.tt..t'" voluo
M . 'oteh .,1.0 not t. IO-IIOS ro.,o
A . AoJocto"l A. "cco,toblo.wlth "u.tl'leotlono,
V - Voltd
-------
..,
0/
..
Total
Surfaae Water
"eta Is Saapling
Results
SOUTH WALNUT CRBBE
Slot Ion 08to Cob. It Copper Iroft 10.11 Llt.l- ........1- ........... Norcllr.. MoI..Wo..-
M-.r '_1M (Co). t ot.1 I (C.). toto 1 (Fe), toto 1 ('b). tot. I (LI). toto 1 ("I). toto 1 (""). tot.1 (lit). toto 1 (Me). 'otol
../1 ../1 ../1 ../1 ../1 ../1 ../1 ../1 ../1
--
SW-OIII 07/21/17 Ineuttlelo.., '_'0 or 10to1 ...to" Anel..e II ..0' rOIlluo.'M.
SW-OM a/.o/. 0.010 U 0.021 U '.0 0.008 U MI 24 .70 0.0002 U ...
SW-OM 04/U/" .0100 U V .0471 A 21.10 A .OJH V .0211 V .... V .280 A .000' V .0"1 "
511-0111 05/11/" . 0500 U A .0210 U A 12.10 V .014' V .0111 V 21.10 V ..7. V .0002 U I .0100 U V
SW-OIII a/07/.. .0100 U V .012' A 1.88 A .0124 V .100 U I 10.70 A ..47 A .0002 U " .100 U V
SW-OM 01/12/" .0500 U I .0210 U A 1.10 V .0010 U A .100 U I 22.'0 A .144 V .0002 U " .100 U V
SW-OM 08/0./.. .0100 U V .0110 U V '.82 A .OUI A .100 U V 22.80 " .1411 V .0004 " .100 U "
SW-O" "/14'1' .0500 U V .0210 U V .4" V .0050 U A .100 U V 18.10 V .471 V .0002 U " .100 U "
511-051 10/1"" Oete "ot ..ot ree.'".'
511-0111 II/IS'" 08to not ..ot rle.t"..
5W-OSI 12/"'" Oeto not ..ot rocolved
5W-OSI 01/25/.0 0.,. not ..ot rlc.lvld
5W.OSll 02/22/10 Oe'e not ..ot rlc.tved
511-0511 OJ/21"0 Duo not ..ot rlcll"..
511-0110 0,/21/., 1.....Hlelo..t 58....10 or 'otol ...tol. A..el..ele ..0' rOIlluo.'M.
sv-ao 11/11'" l..euHlelo..' '_10 or 'otol Notol. A..ol..e" "t rOJllUOe'M.
SW-OIIO 07/01/88 0.050 U 0.025 U 0.100 U 0.001 U ... 17 0.011 U 0.0002 U ...
511-060 OJ/II/II .0500 U A .0210 U V .100 U A .00110 U A .100 U V 11.10 V .0114 A .0001 U " .100 U "
511-060 OJ/II/.. .0100 U A .0210 U V .100 U " .0050 U A .100 U " 11.10 ' .0110 U A .0001 U " .100 U "
511-010 05/11/.. .0100 U A .0250 U I .100 U V .0050 U II .0100 U V 11.80 " .0211 V .0002 U I .0100 U "
sw-ao 05/1./.. .0500 U A .0250 U I .100 U V .0010 U A .0100 U , 12.80 ' .0212 V .0001 U I .0100 U V
sv-ao a/o./.. .0500 U II .0250 U II .'14 " . 0010 U A .112 " ".80 II .0"' " . 0001 U " .100 U "
sw-ao 07/0./.. .0100 U V . 0250 U " 1.12 V .0050 U " .100 U II 11.40 V .0288 V .0002 U II .100 U II
sv-ao 08/0J/.. .0500 U V .0250 U I .1.7 V .0010 U " .100 U V 17.10 V .0110 U II .0002 U V .100 U V
511-0110 0'/11'" Oeto ..ot ..ot rlc.lvld
511-0110 0./11'.. 08to ,;ot ..ot rlcllv..
SW-OIO 10/0./.. .0200 U V .0200 U V .0855 " .0020 U V .0200 " 11.70 " .0100 U II .0002 U " .100 U V
SW-OIO 11/01/.. D.to not ,I' rlcll"..
511-010 II /0"" Oeto not ..ot rlcllv..
SW - 010 12/0./.. Do to not ..ot rlcll"..
511-0110 01/2J/1O Oeto ..ot ..ot rlc.t".4
511-0110 02/0./10 Ooto not ..ot rlcllv..
SW-OIIO OJ/12/1O Ooto not ..ot rlc.tv..
SW-OII 0'/22'" In,uttlc lo..t 58....10 or 'otel Hotol. "nel...le ..ot rOIII...etoll.
VALUE QU"llfIEIS, MI. "...I..to .ot roportoll U . "nol...od but not lIotoctM
J . 'ro,ont bolow lIotoetlon 11.lt I . 'rooont In 10borotor.. bl...b
DAIA VAllDAllON QUAlflEAS, (No v.lll1otlon qll.lltlor Indlcoto. dote hoe not boon ..elldotoll.)
. - NoIIII.. 'I.. .01 ..t I - letl..toll ..01...
M . lotc. .,Ibo not I. 1O-11Ga re..o
-------
".. ~
Surface Water
Total Metala Sa.pling Re.ults
SOUTH WALNUT CRBBK
Stetton Oah Hlch' Pot..a'''' 5o'onl- Stlvor
Mu.ber Sa.p'od (HI), toto' (It ). tout ($0). toto' (lit). tot01
.'/' ../1 "/' ../1
------ ------ --.---
SW.OSI 01/21/81 Ina..flle'ont 5_'8 or 10to' Moto'a Ana'ra'a not ro~..oatod.
SW-OH "/JO/.. 0.080 U a.o U 0.005 U 0.010 U
SW.OSI Ol/U/" .0100 U A I.oa A .02&0 U A .0100 U V
SW-OS' 05/"/8' .0100 U . IU II .0050 U " .0100 U .
SW-OS' 0'/0' /8. .0100 U " IU II .0050 U " .0100 U "
SW-OS' 01/12/.. .0100 U V IU . .0050 U . .0100 U "
$V.OS' 08/0./.. .0100 U V IU V .0050 U " .0100 U "
SW-OS' 0./11/8. .0100 U . au . .0050 U " .0100 U "
SW-05' 10/18/8. Ooto not rot recetved
SY-OSI 11/15/" Doto lIot ..ot rocolvod
SW-OSI 12/1./.' O.to lIot ..ot recetved
SW-051 Ol/U/.O Oato "ot ..ot rec.lved
5Y-OSI 02/22/10 Det. ..ot rot received
5Y-051 OJ/21/1O Oato lIot rot received
SW-OIO 07/21/87 Inaufftcto"t 5.""0 or 10tol Motol. ""alra'a lIot ro....oata..
SW-"O 11/11/.7 I"...'"ctollt 50..,10 or 10tol Motolo ""01".'0 IIOt ro..uo.to..
SW-O'O 07/01/.. 0.010 U !I.O U 0.005 U 0.010 U
SW-OIO 01/ 11/.. .0800 U A au " .0050 U " .0100 U "
'Y-OIO 0./11/.. .0100 U A IU II .0050 U " .0100 U "
'Y-OIO 05/11/8. .0100 U . au . .0050 U " .0100 U A
SW-OIO oS/la/.. .0100 U . au A . 0050 V " .0100 U "
SW-OIO 01/0./8. .0100 V " au " . 0050 V A .0100 U II
SW-OIO 07/01/.. .0100 V " au V .0050 V . .0100 U .
SY-OIO 08/0J/8. .0100 U V !IV V .0050 U " .0100 U V
SW-OIO 0./11/8. Ooto lIot ..ot roeolvod
SW-OIO 0./../8. Doto lIot ..ot rocolvod
SW-OIO 10/0./.. .0200 U V .628 " . 0020 V V .OJOO V V
SW-OIO "/"/" Doto "ot ..ot rocolvod
SW-OIO "/"/" Oato ..ot ..ot roco'vod
SY-060 11/"/8' Doto lIot ..ot rocolvod
SW-OIO 01/"/" Oete "ot ,et received
SW-OIO 02/0'/" Oah "ot yet received
SW-OIO OJ/ "/" O.t. "ot yet rec.lved
SY-Ol! 07/22/8' 1".uHlclont S.mpl. or lotol Motoll An01,,"lo lIot ro..uo.tod.
VALUE QUAllfl(AS; HA. Anal..to "ot roportod V . A"a'...ad but "ot .atoetod
J . Proao"t "'ow .otoetlo" 11.lt . . Pro.o"t I" '...rotor.. .1011'
DA1A VAlIDA110N QUAlfl£A5: (Ho valldatlo" quallflor I"dlcato. da.o haa "ot boo" v01Idatod.)
S..I- Stronll- 1110111- "" V...a.'-
(No). toto 1 (Sr). totol (11). toto1 (S,,). 10tol (V). totol
../1 ../1 ../1 ../1 ../1
IS 0.' 0.010 V III 0.050 V
1.1' V IV V .0100 U . .100 U V .0111 V
51.80 V IU , .0100 U II .100 U V .0&00 U V
&1..0 " .611 " .0100 U II .100 U V .0&00 U ,
IS.IO " IV . .0100 U V .100 U , .0&00 U A
&8.20 V IV V .0100 U V .100 U V .O!IOO U "
".10 " IV V .0100 U II .100 U , .0- U V
" 0.' 0.010 U III 0.0&0 V
JO.10 " .al' V .0100 U " .100 U V .0100 U V
11.10 " .au V .0100 U A .100 U " .0&00 V V
JO.'O V IV V .0100 U A .100 U V .0500 U V
JO.IO " IU V .0100 U II .100 U , .0500 U V
28.10 V IV V .0100 U II .100 V V .0500 U A
" , IU II .0100 U . .100 U A .0500 U V
12.20 V IU V .0100 U A .100 V V .0500 U V
27.10 V .&20 V .OOJO V . IV A .0100 U V
. - Hot.I... II.. lIot ..t I . hU..ted vol"o
N - 'otell 0,1'0 "ot I" 8O.120S ro...o
. . AoJocto.1 A. Aceo,ta.lo .Itll ....ot't'cot'o".1 V. Val'.
'"
-------
Total Ketala
surtace Water
sa.pling Re.ults
SOUTH WALNUT CRRRE
Statton OaU line
"_or SalOp '001 (In). toUI
"'/'
-~--
$V-OSI 01/21/11 l"auUlelo"t S_'. or fota' M8ta', An.'y'" Rot requ......
$W-OI' OI/JO/88 O.OJO
$V-OSI 04/ U/I. .201 V
$V-OSI 05/11/1' .0J87 A
$V-oa. 01/01/1. .0111 A
$V-OSI 01/12/1' .OUI V
$V.ola 08/0'/~' .On2 A
$V-ola 0./14/1. .108 V
$V-ola 10/11/1' Olt. not rat recetved
$V-051 11/15/1' OOU "ot .ot reca'v."
$V-051 11/1./1. OaU not .ot recatved
$V-osa 01/25/10 Oa'e not .ot rac.lva.
$V-051 02/22/10 0.,. not .ot recalve.
$V-osa OJ/21/1O OoU "ot .ot recatvaet
$V-060 01/21/11 InluUlclont S...,. or IoU' ....... A,,"'.a.. lOot ro"uoato..
511-010 11/11/11 1""uUlelo,,t SOlOplo or 1018' "'18.. A"a"a.. "ot ro"uoato..
$W-oao 01/01/88 0.400
$V-OIO OJ/II/.. .J" V
$V-OIO OJ/I./II .41' V
$V-oao 01/11/1' .JII A
$W-oao 05/11/11 .Joo A
$V-OIO 08/0./11 .518 V
$V-OIO 07/01/11 .150 II
$V-OIO O./OJ/.. .'Z71 V
511-010 0./11/.. 0018 "ot .ot reeetve.
$V-oao 0./11/11 0018 lOot ,ot roeotvo'
$V-060 10/OJ/.II .411 V
$V-oao 11/08/11 0018 lOot .ot racel"I"
$V-OIO 11/01/11 Oota "ot .ot roeotvo'
$V-060 11/01/11 0018 lOot .ot rocel"o.
$W-060 Ol/U/IO 0018 "ot )/ot recelva.
$V-D60 02/01/10 Data lOot ,at racllva.
$V-oao OJ/12/1O Ooto "ot .ot ree,'ved
SV-061 07/22/.1 I,,"u'''clont SaIOp'o or lotol "'ta'" A"al)/ala lOot roquoato'.
VALUE QUALifiERS: HA - A"a',.o "0' roporto. U - Anol,.od but lOot .otoctod
J - Pro.o"t bo'ow .otoctlo" 11.lt I - Pro.o"t I" laboratorr blo.'
DAIA VALIDATION QUAlfl(AS: (No vol Ida. 1o" quoll'lor Indlcltol dote haa "ot boo.. ,,011010'0..)
. - "'1.'... tI- lOot _t 1 - la..-t.. ...Iuo
" - latch 0'''0 "ot ,,, .-11IWo ro",o
. - 'oJoc.o.. A - Aecoptoblo with "uoll"cotlo"a,
..
V - Va".
-------
8urfaae Water
Total .etals 8..pling Results
80UTH WALNUT CRBBK
Station Ooto A,....tnu. lint I_n, . Ar..ntc lerl- hr,IH- Co...1- Colcl- C..I- Cllr_l-
N-er 5_led (AI). totel (5"). '0'01 (A.). to'ol (h" 'otol (h). 'otol (Cd). to'ol (Co). 'otol (C.). '0'01 (Cr). toto 1
..'I .." .." ../1 ../1 ../1 ../1 ../1 ../.
-.-- --
$W-OII 11/"/17 1"...Ulclo,,' 5...'. or loto' Mo.oI. Anol,.I. IIot ro.....'od.
$W-OII 07/01/" 0.200 U 0.060 U 0.010 U 0.100 U 0.005 U 0.005 U t7 NIl 0.010 U
SV-OII 01/20/1' 1.11 II _~00 U A .0100 U II .100 U II .0050 U II .OOSO U II 27.40 II IU II .01" U II
$W-OII 05/15/1. .zoo U II .~00 U II .0100 U II .100 U II .0050 U A .0050 U . ".10 V IU " .0100 U A
SV-OII 01/0./8. .100 U A .0100 U " .0100 U V .200 U A .0050 U A .0050 U . 84.50 A IU " .0100 U .
SV-OII 07/0./8. .281 A .0100 U " .0100 U " .100 U " .0050 U V .0050 U " to.SO " IU " .0100 U II
SV-OU 08/0./8. .111 II .0100 U II .0100 U II .100 U A .0050 U II .0050 U " 84.10 " IU " .0100 U II
SV-Gel 0'/"/8' D.'. not ..e' received
SV-OII 10/0./8. .U5 II .500 U " .0020 U II .170 II .0020 U II .0040 U II 87.10 II .0010 U II .0200 U II
SV-061 10/20/" OR'
SV-O&I 11/01/" Doto no' ret received
$W-O&I 12/01/.. Dote "0' ret rece'veel
$W-O&I 01/2./tO Dote "ot '0' rocotvod
SV-OII 02/0./tO Doto "0' '0' rocotvod
SV-OII 01/12/.0 Doto IIot ,ot rocotvod
SV - 061 01/12/10 Doto "ot ,ot rocolvod
SV-IOI 01/ .0/.. 20.0 0.0'0 U 0.010 U 0.100 U 0.005 U 0.005 U II NIl 0.010 U
$W-IOI 04/ ../.. Doto "0' ,ot rocolvod
SV-IOI 05/11/.' 2..10 II .0100 U A .0100 U II 2.02 " .0572 A .0142 A 152 " IU " .212 A
SV-IOI 01/07/.' 1.77 A .~00 U " .0100 U A .100 U " .0050 U " .0050 U " ..... " .100 U " .0108 U "
SV-IOI 07/12/8. -500 A .0100 U " .0100 U II .100 U " .0050 U II .0050 U " 7.71 " IU I ..100 U II
SV-IOI 08/0'/.' 2.85 II .0100 U II .0100 U II .100 U " .0050 U " .0050 U " 11.70 " .100 U " .0100 U V
SV-IOI 01/../.. .200 U II .0.00 U A .0100 U V .200 U " .0050 U " .0050 U I 7.'4 " IU " .0100 U .
SW-.IOI 10/11/.' Dote IIot ,ot rocotvod
$W-IOI 11/15/8. Ooto "ot ,ot rocotvo.
SV-IOI 12/1./.. Ooto "ot ,ot received
5W-101 01/25/.0 Ooto "ot '0' rocotvod
5W-101 02/22/10 Doto IIot ,ot received
SV-IOI 01/2 I /to 0.'0 not '0' rec:.lved
"ALU[ QUAL If lEIS, NIl. A"ol,to "ot roported U . A"ol,.o. ....t IIot .otocted
J . Pro.o..t "olow .o.octlo" 11.1. I. Pro.o..t I" '.lIorotor, "10.'
DATA YALIDATION QUALfIEA5: (No ...11.0.10.. quollflor Indlco'o. do.o h.. "ot boo" "0.1.0'0..)
. - Mol.... tl- "ot ..t I . 1.'1_'" vo....
N - lo'cll .pI'o "0' I" 80-1201 ro..o
. . "Iocted. II. Accopto"'o .Itll .....lflc.tlo".1 II - "~'I.
.,
-------
--.
..
Total
Surface .ater
"etal. Saaplinq
Re.ult.
SOUTH WALNUT CRBBK
Statton 0.'. Coboll Copper Iron loo. lUIII- Mo,nool- Men.onooo Morcllr, MoI,wo..
"_or 5o..,lod (Co). toto I (CII). to.ol (fe). tohl ('b). totol (u). toto I (HI). tohl (....). tohl (H.). tohl (Me). '0'01
89/1 ../1 ../1 ../1 ../1 89/1 ../1 ../1 ../1
-- .---- ----- ---.---
SW-061 11/11/87 Inouttlclo.t 50..,10 or '0181 Motol. Anol,olo not roquooto..
SW-061 07/01/88 0.050 U 0.02!1 U 0.'0 0.001 U HR I' 0.08 U 0.0002 U till
SW-061 0'/20/89 .0500 U A .0250 U V 1.1] V .02110 U " .100 U V 1.7' V .0'" II .0001 U II .100 U II
SW-OII O!l/I!I/89 .0500 U " .0250 U . .165 II .01!lO U II .0100 U II ".80 II .0108 II .0001 U . .0100 U II
SW-061 06/0'/" .0500 U A .0250 U A .1" V .0050 U A .100 U II n.80 A .0..1 II .0001 U II .100 U "
SW-061 07/01/89 .0500 U V .0250 U A .'11 V .0050 U " .100 U A ".50 V .OU, II .0001 U A .100 U A
SW.OI. 08/0./.1 .0500 U V .0250 U . .120 V .0050 U A .100 U II 1!I.50 .ON5 II .0001 U II .100 U "
511-061 0'/11/" Oe'a not ,et racat".d
SW. 061 10/0'/" .0200 U V .0200 U V .817 V .0016 II .0210 A 16.50 V .0571 II .0002 U A .100 U V
SW-061 10/20/" DAY
511-061 11/01/" Doh not ,ot racatvad
511-061 12/06/" Doh not ,ot racatvad
SW-061 01/2'/90 Doh nol ,ot racetvad
SW-06. 02/09/.0 O.t. "ot ,at raceivad
511-061 0'/12/90 Dolo not ,ot recetved
511-061 0./12/90 Dolo not ,ot racalvad
SW-IOI 06/JO/88 0.050 U 0.025 U 15.0 0.010 HR 1.0 U .n 0.0002 U till
SW. 101 ol/n/.. Oet. not ya' racalvad
SW-IOI 05/11/" .n2 A .2n A 201 V .215 II .IU II ".70 II 1.68 II .002' A .171 V
SW-IOI 0'/0'/" .0500 U " .0J48 A 2.n A .0400 U II .100 U . IU II .UI II .0001 U II .100 U II
SW-IOI 07/12/11 .0500 U II .0250 U . .8!11 V .0050 U II .100 U . au II .0110 II .0001 U II .100 U II
511-101 08/0'/" .0500 U V .0250 U A 5.20 II .00!lO U II .100 U A au II .I!I' II .0001 U " .100 U II
SW-IOI 0./ "/" .0500 U V .0250 U II .J57 II .00!lO U A .100 U II IU II .01S0 U II .0001 U II .100 U II
511.101 10/ "/" Doh not '0' racetved
511- 101 II/I!I/" Doh not '0' raeatva"
511-101 12/19/" Doh not '0' raeatvad
SW-IOI 01/25/90 Doh not '0' rae.tvact
SW-IOI 02/22/90 Doh not ,ot raeatvad
511-101 0'/21/90 Doh not ,ot racalva"
VALUE QUAllfl[R5: HR - Anol,to no' roporto' U - Anol,.od but no' 'o'oc'"
J - 'ro.ont bol.. .otoctlon 11.1. 8 - 'rooon' In 10boro'or, blonk
0"'" V"LIO"IIOH QU"lfl[A5. ("0 volldotton quollflor Indleotoo doto hoo not boon votl.oto'.)
. - HoI.I., 'I.. not ...t I - lotl"'o. wotuo
H - ao'e" o,lko no' In 8O.11Oa ron,o
. - AoJocto., ,,- Aceoptobto .1'" quott'teottono.
-------
Surface Water
Total lIetals
s88plinq Results
SOUTH WALNUT CRBBK
Stat Ion 0.18 Hlch' Pot..a"" S.'.nt". SlIvor Sodl.. Stront I.. '''a II I.. fI.. Vo..a'l..
H-llar Sa....lo' (HI). total (It ). 'otol (So). totol (A,). total (Ho). totol (Sr). toto I (n). 'oto' (Sa). 'ota' (V). 'otol
--./. ../. --./. --./1 ../1 --./. --./. ../. ../1
-.------ --
$V-Oil' 11/11/17 Ina..Ulclo..t 50""'0 or loto' ~t.'. Ana'ya'. not requ..tad.
$V.OII 0'/01/11 0.0'0 V $.0 V 0.005 V 0.010 V J2 0.110 0.010 V NA 0.050 V
$V-Oil 03/20/89 .0.00 V A 5U A .0050 V A .0100 V V ".SO V .205 V .0100 U . .100 U V .0100 U V
$V-OIl 05/15/19 .0.00 V . tIU A .0059 A .0100 V A 32.20 V IV V _0100 V " .100 V V .0100 V V
$V.OIII 011/09/19 .0.00 V " tIU " .0050 U " _0100 V " 30.30 V IV V .0100 V " .100 V V .0500 V .
$V-OIl 07/011/19 .0.00 V " 5V V .0050 U A .0100 V A 29 V IV " .0100 V II .100 V " .0500 V V
$V.061 08/03/19 .0400 V V 5V V .0050 V " .0100 V V 30.90 V IV V .0.00 V V .100 V V .0500 V V
$V.061 09/11/19 Oato not Ifat receIved
$V - 061 10/03/19 .0200 V V 1.27 " .0020 V V .0300 V V 30.60 V .520 V .0030 V A IV V .0100 V V
$V.061 10/20/19 OAY
$V - 061 11/06/89 O.ta "ot yet received
SW.OIII 12/011/19 Oa'a not )"at recetvad
$V. 011 I 01/23/90 Data not Ifa' rlcelved
$V. 0111 02/09/90 Doto not Ifot received
$V-061 OJ/12/90 o.to not Ifat roco tv.d
$V-OIl OJ/I2/90 o.to not Ifot received
$V. 101 06/30/88 0.0'0 U 5.0 U 0.005 V 0.010 V . 0.200 V 0.010 V ... O.OSO
$V-IOI O./U/II o.ta not ,et rlcelvld
$V-IOI 05/11/19 .245 " 21. 50 V .0050 U " .0117 " '.10 V IU V .0100 U " .100 U V .$55 "
$V-IOI 06/07/19 .0.00 U " 5U " .00110 U V .0100 U " II." V .100 V V .0100 V V .100 V V .01100 V V
$V.IOI 07/12/19 .0.00 V V 5U A .0050 V A .0100 V " 11.15 " IV II .0100 V V .100 V II .0500 U V
$V-IOI 01/0./89 .0400 V V 5U V .0050 U V .0100 V V tIU V .100 V V .0100 V V .100 U V .0100 V V
SW-IOI 09/14/89 .0.00 V A 5U A .0050 U " .0100 U " tIU V IV V .0100 V V .100 U V .0100 U V
$V-IOI 10/11/89 0.18 not ,at rec.lvld
$V-IOI 11/11/19 0. to ..ot Ifat rocolva'
SW-IOI 12/11/89 Doh not Ifat rocolvod
SW-IOI 01/25/90 0.,. "ot ret rae.eyad
SW-IOI 02/22/90 0.,. not ,at recalvld
SW-IOI OJ/21/90 Data not 'It received
V"LUE QUALifiERS: HA. Ana'Ifto not roportad V . Anollf.od b..t not 'otoc'od
J - 'r...nt _.10. ..tlctton I'.tt . - Pr...,,' In 1.~or.tor, ~'.n'
OAf A VAt IDAf ION QUALfIEAS: (No voll..tlon quall'lar In'Icat.. '.ta .... not boa.. va'ldato..)
. . Ho'''.., tt- not _t I . Iott_to' va'"o
N . 'atc" .pl.o no' I.. to-12~ r...,o
II . A.Jactod: A. "ccopt....o .1'" quall'Ic.tlon.:
V . Volt.
,.
-------
SOUTH WALNUT CRBBK
St.tton 01'.
H""bor 50..lod
._. ---
$W-061 11/11/87
$W-061 07/01/88
$W-061 03/20/11
SW-061 Or./15/8.
SW-061 06/0./11
$W-061 07/06/8.
SW-061 08/OJ/89
$W-061 09/11/8'
$W-061 10/03/8'
$W-061 10/20/11
SW-061 11/06/8.
SW-061 12/06/89
SW-061 Ol/U/IO
$W-061 02/0./10
$W-061 03/12/90
$W-061 03/12/90
SW-IOI 06/30/88
$W-IOI 04/ U/8'
SW-IOI 05/11/..
SW-IOI 06/07/8'
$W-Iol 07/12/8.
SW-IOI 08/09/8'
$W.IOI 0./14/8.
SW-IOI 10/18/8.
SW-IOI 11/15/89
SW-IOI 12/11/89
$W-IOI 01/25/.0
$W-IOI 02/22/'0
SW-IOI 03/21/'0
lInc
(In). toto I
.,/1
-------
"..,
Surface Water
Total Metal8 sa.pling Re8ult8
Inou"lclont 50..18 or 'otol Hotolo AnolYll1 not roquootod.
0.140
.JOII
.0.17
.267
.207
.195
A
A
V
A
V
0.'8 not ~.t rec.lved
.203 V
DAY
o.to not yo. received
o.to not yot roco"'od
o.to not rot rec.lved
0..0 not rot received
0.'8 not yo. rec.lved
Do to not yot received
0.100
0.'8 not yet received
"" A
.141 A
.0200 U A
.0501 V
.0200 U A
0. to not rot
Doto not rot
Doto not rot
Doto not yo'
Doto not rot
0.'8 not r.t
received
received
received
rec.'ved
received
received
VAlU[ QUAllfl[AS, HA - Anolr'o nat ropor.od U - Anoly.od bu' no' dotoct..
J . Pr...nt below detactlon ".It . - 'r...nt 'n '.'ore'er. .'8ft'
OATA VALIDATION QUALfl[AS: (No vol Idol Ian qUIII'lor Indlcotoo dote hoo not boon vilidotod.)
. - Noldl.., tI- ..ot _t I - lotl_tod vol..o
M . '.tc~ 1_". not In 1O-120S raR,.
. - AoJoctod; A - Accoptlblo .It. q..olltlcotlono;
~
..
-------
STATION 5'
Stet Ion
N_ar
$\I-OS'
$\1-05'
$W-05'
$W-os.
$W-05'
sw-os.
$W-05'
$W-OS'
$W-OS'
$W-OS'
$W-OS'
$W-OS'
$W-os,
sw-OS'
0.'.
SaMplad
------
07/21/87
07/01/88
03/20/89
05/11/8'
0"08/8'
07/08189
08/10/"
0'/18/"
10/0)/"
II 10'/"
12/08/"
01/2)/'°
02/°'/90
0)/12/'0
Surface Water
Total Metals Sa8plinq
Results
"I_ln- "n"_ny' Ar..n'c lerl- ler,"I- Ca.l- Calel- c..t... Chr_l-
("I). total (SIt). t...1 (".). to..1 (Ia). total (Ie), to.. I (Cd), to.. I (Ca), 'otal (c.), to..1 (Cr), 'otal
.../1 I "'/' M9/' ..'I .." ..'I .." ..." ..."
----- --~---- --- ---
Inlu'tlelent Sa..'a or To" 1 Ma" It "n.I,. It not ra"u..t"'.
..) 0.060 U 0.010 U 0.200 U 0.005 U 0.005 U 121 NA 0.010 U
Lit V .0600 U A .0100 U " .208 V .00110 U A .00110 U A II' " IU V .0100 U A
12-10 V .0600 U " .0100 U " . UI II .0078 " . 0050 U II eI. " IU " .0232 "
1.21 V . 0600 U " .0100 U A .200 U " .0050 U " .0050 U " III " .100 U " .0100 U "
1& " .101 " .0100 U " .481 II .0057 " .ooso U " In II .100 U II .0147 "
0.'8 not yet received
.200 U A .0600 U Y .0100 U Y .200 U V .0050 U " .OOSO U V IU " IU Y .0100 U Y
.ltO V .500 U Y .0020 U Y .11' " .0020 U V .0040 U " 101 " .0010 U Y .0200 U Y
Data not yet rec.'v.d
0.'. not )let rec.'veel
Da" not ,at received
D... not ,at received
O.t. not ,at received
. - MOI".I tloo not oot 1 . I.tloota' velue
N - latch .plle nat In 1O-12aa ranla
II - AaJected; ". "c.eptahla .Ith "uall'l.atlon.;
V"LUf QU"LlflfRS: NA. "nal,te not reported U . Anal,.ed hut not 'ataeta'
J - .r.'.ftt ..10. d.tectlon ...It . . 'r...n' In '.~r.t.r, bleft.
DAI8 VALIDA I ION QUAlflfAS: ("0 validation quall'lar Indl.ate. data ha. not baan validated.)
V . Vall'
~
-------
STATION 59
Stet'on
"w.blr
SW-05'
SW.05.
5\1-051
5\1-051
5\1-05'
5\1-05'
5\1-051
5\1-05'
5\1-05'
5\1-05'
5\1-05'
5\1-05'
5\1-05'
5\1-05'
De'.
5..,lod
------
07/21/87
07/01/.
01/20/89
05/11/8'
01/01/8'
0'/08/11
08/10/11
0' /11/11
10/OJ/II
11/01/11
12/01/11
Ol/U/IO
02/0"10
OJ/12/1O
Cob. It
(Co). tohl
..'1
1...uUlelo..t
0.050 U
.0500 U V
.0500 U A
.0500 U V
.0500 U V
Coppor '
(C..). total
..'I
s...,o or Toto'
o.on U
.0250 U V
.0250 U A
.0'" A
.0417 V
08'8 not yet racelved
.0500 U V
.0200 U V
0.'1 not
Doh ..ot
O.t. not
Data not
Oa'a "ot
.0250 U V
.0200 U V
rat racelved
.ot roul vod
,..t rec.I"ed
.ot roulvod
rat rlcalvad
,"'"
....
lood
(,It). totol
../1
V
V
V
A
r...y..tad.
0.001 U
.0JI7 A
.01" A
.0010 U A
.0258 A
Surface Water
Total Metals saaplinq aesults
Iron
(fo). tohl
../1
Motol. A..ol..I. ..ot
5.0
1.11
17
.845
16.10
.100 U V
. J25 V
.0050 U V
.0020 U A
VAlU[ QUALlfl[A5: HA - A..ol.to ..ot roportod U - A...I..od It..t ..ot dotoetod
J . 'ro.o..t bolow dotoctlo.. 11.lt , . Pro.o..t I.. 'o\torotor, Itl....
DA'A VAlIDA'ION QUAlfl[AS: (Ho volldotlo.. quoll'lor I..dlcoto. d.to h.. ..ot boo.. volld.tod.)
ltthl-
(Lt), tohl
..'I
Mo,nul-
(He). toh 1
../1
Mo",."ooo
(Mo). hto'
.."
MoI"'''-
(Mo). totol
..'I
Morc..r,
(lit). totol
..'I
HA U 0.08 0.0002 U l1li
.100 U V 28.70 V .OUI V .0008 A .100 U V
.0211 V 27.70 V .US A .0002 U II .0111 V
.100 U " 20.10 V .04" V .0002 U V .100 U V
2.5' V 28.40 V .117 V .0002 U V .100 U V
.100 U A 24.50 V .0150 U " .0002 U V .100 U "
.0250 A 21.80 V .0100 U A .0002 U " .800 U V
. . Holdl", tl.. not ..t 1 - l.tl..tOd .01..0
" . 'otch .'''0 ..ot I" 80-12. roll'O
-------
Stetlon 'Oet.
STATION 59
H".".r
sw-OS'
$W-OS'
$W-OS'
$W-OS'
$W-OS'
$W-OS'
$W-OS'
511-0S'
SW-OS'
511-0S'
$W-O!ll
$W-OS'
$W-OS'
$W-05'
50"'Plod
----_.'--
01/21/81
01/01/88
01/20/.'
OS/II/.'
06/08/..
01/06/..
08/10/.'
0./1./..
10/01/.'
11/06/.9
12/06/..
01/21/90
02/09/90
01/12/90
Surface Water
Total Metals S..plinq Re.ults
Nlc..' Pot... tu. . 5010nl- Silver 50dl- Stront 1- 'holll- "n Vonodl-
(HI). toto I (I( ). toto I (50). toto I (",), toto I (HO). total (Sr). toto I (ft). totol (5n). 'otol (V). total
-.g/I ..'I ..'I ..'I ../1 ..'I ..'I ..'I ..'I
.,---- .- ----- ---- --- -----
In.ufflclont 50,.10 or Toto I ""tal. "nol,.I. 80t r...u..tecl.
0.040 U 5.0 U 0.005 U 0.010 U ZI 0.1 0.010 U NIl O.OSO U
.0400 U V 5U " .OOSO U " .0100 U V H.80 V .JlI V .0100 U I .100 U V .0100 U V
.0400 U A !IU " .0160 " .0100 U " 17.60 V IU V .0100 U " .100 U V .0584 "
.0400 U " !IU " .OOSO U " .0100 U " II. 50 " .601 " .0100 U " .100 U " .0500 U "
.0400 U " !IU " .0500 U " .0100 U " 10.50 " I." " .0100 U " .100 U " .05111 V
Oat. "ot ret received
.0400 U A SU A .OOSO U A .0100 U " 14..0 " IU " .0100 U " .100 U " .0Soo U V
.0200' U " .811 " .0020 U V .0100 U V ]0.10 V .6U V .00JO U . IU V .0100 U "
O.ta no' ,ot received
Data not ,ot r.celv.d
Oat a not ,e' received
Da'8 "ot yet'recetved
Oat. "ot yet recelv.d
VALUE QUAllfIEAS: HA. Anol,to not roportod U . Anol,.od but not dotoctod
J - Prooont bolo. dotoctlon 11.lt . . Prooont In lo'orotor, blon.
PA'A V"lIDA'ION QU"lfIEAS: ("0 valIdatIon quoltflor Indlcoto. data ho. not boon v.'ld.tod.)
. - 1Io'lIln, tI- not _t ( - htl_to" volu.
" - 'otch 0,1.. not 18 10-1201 ron,o
I - AoJoctod, ,,- "ccoptoblo with quoll'lcotlono,
V - Vall"
..,.,
-------
STATION 59
Stet'on
".-b.r
swoon
SW-05'
swoon
SW-05'
sw-on
SW-05'
sw-on
sw-OS'
SW-OS'
SW-05'
SW-05'
SW-05'
SW-05'
SW-05'
0.'.
So.plod
n-..'------
01/21/87
01/01/1'
OJ/20/11
05/11/11
06/0./11
01/06/11
08/10/89
0'/18/11
10/03/11
11/06/89
IZ /06/89
01/23/'0
02/0'/'0
OJ/12/'0
-"\
Surface Water
Total Metals S.-pling Re8ults
ZInc
(In). tohl
../1
.-----
Inoufflc'ont 50..10 or lotol Metolo A"olyo'o not roquootod.
0.500
.513 A
1.08 A
.U3 V
2." V
0.18 not ,ot
V
V
received
.2)'
.2ot
0.'. ..ot
o.to not
DOh not
Do" not
Oete not
,et received
,e' received
,et rece'v.d
,et rec,'ved
,et received
VALUE QUALIFIERS: HA - An.1yte not reported U - An81YE8d but not ~.t.ct.d
J - Pr.....t beto. ..'actton It.'t . . Pr...nt 1ft t..or.terr .....,
DAIA VALIDA I ION QUAlfIIRS: (No yolldotlon quollflor Indlcoto. doto hoo not boo" Yolldotod.)
. - Ho'.'". tt.. not -t ( . (1,I_t.. ".'u.
N - lotch opl.o not 'n 8O-12~ ron.o
A - .0Joctod; A - Accoptoblo .Ith quollflcotlo"o;
~,
....
-------
STATION 63
St.tton O.t.
NU8bor So.,lod
N-OU
N-OII
N - OU
511-061
N-OU
N-OU
511-061
511-061
511-061
511-0U
511-061
511-06J
511-061
------
07/24/87
07/01/88
01/28/81
05/12/89
06/21/89
07/19/89
08/11/89
09/15/89
10/04/81
II/OJ/89
12/01/89
01/05/90
02/02/90
AI_tn-
(AI), toul
../1
------
"'0,
Surface Water
Total Metals Sa.pling Results
A..tt_..;
(n), UUI
../1
hrt-
(10). toUl
../1
A,....ntc
(Ao), toU I
../1
-------
-- ---_.------
I..,uffleto..t So,,'o or lotol Hotol. Anoly,t. ..ot roquo.tod.
0.600 U O.OOJ 0.107
0.750
ORY
ORY
ORY
ORY
ORY
ORY
DAY
DAY
DAY
DAY
ORY
VALUE QUAllfIEAS: NA - A...lyto ..ot roportod U - A..oly.od but ..ot .otoeto.
~ - Pr...nt be'ow detection ".'t . - 'r...n' In '.'.rater, ~,.ft'
OAIA VALIDAtiON QUAlfIEA5: (Ho v.lldotton quoltflor Indte.t., d.lo h.. not boo.. voltdot.d.)
I.ryllt- C...I- Colel- C..tt81 C"r_t-
Clo), toto I (U). toU' (C.). tot.' (Ct). tot. I Cer), t.U'
..I' "/' ..I' ..I' "/'
----- -----
0.002 U 0.004 U '4.& HA 0.020 U
. - Ho'.'nl tt.. not ..t I - I.tt..t.~ valu.
N - I.tc. apl'. Rot In 8Q.IIOS rln..
A - AoJoetod; A - Aecoptoblo wit" .v.llfleotlon,; V - Volld
~.
-------
STATION 63
Stetlon Oat.
Huebor So,,'od
$V-ou
$V-OU
$V-OU
SW-06J
SW.OU
SW-OU
sw.on
SW-06J
swoon
sw.on
SW-06J
5W.06J
swoon
07/24/87
07/0./88
0]/21/88
05/12/"
06/21/81
07/"/11
01/11/81
01/15/81
10/04/81
11/0]/11
12/01/"
01/05/10
02/02/10
Cobo It
(Co). loh'
M,/I
-----
Coppor
CC..). '01.'
../1
Total
Iron
(fa). 101. I
../1
-----
surtace Water
Metals SaaplinCJ
Lod
C'.). tohl
../1
1"...rrlel.,,1 5...1. or ToI.I He'o'o A"ol,olo "0' r.~"ol'od-
0.020 U 0.020 U I. J2 0.001
DRY
OIlY
DAY
OAf
DR'
DR'
DR'
OAf
OAf
DAY
DA'
VALUE QUAllfl[AS: HA. A,,".,Io "0' r.porlod U . Anl',.od b.., "0' ~.'.e'o~
J . Pr..."t ~..~ detect ton I'.tt . . 'r...nt In 'aboretor, ~,."k
DAIA VAllDAIION QUAlfl[AS: (No "o'Ido'Ion qUlllrlor '"dleoloo dll. ho. "01 boo" ,,".1.0'0..)
Ltthl-
CLt). toh'
../.
Results
HeI"U'-
("'). tot. I
../1
HA
J2.0
"-nl'''.'.
C...). toh I
../1
0.415
"1t.
"'rcurr
(Nt). tohl
../1
0.0002 U
. . "'I~I"I ,,- ..0' _t I . 10"_'''' ".1"0
H . elteh .,1'. "0' ,.. 1O-IZoa r.....
. - A.Joetad; A. Ace.,t.b'. .tt. ~w.ltftc.t'on.1
V . V.""
...
MoI,Wo..-
(Mo). 'otll
../1
-------
STATION 63
5..tlo"
N.-er
$\I-OU
$\I-OU
$\I-06J
$\I-OU
$\I-OU
$\I-OU
$\I-05J
$\I-06J
$\I-OU
$\I-OU
SW-05J
$\1- OU
$\1-06)
Oat.
So.plod
....------
01/24/81
01/05/88
OJ/21/1'
OS/12/"
OS/21/"
01/"/"
01/11/"
O'/IS/.'
10/0./.'
II/OJ/.'
12/01/8'
01/05/'0
02/02/'0
Nldol
(NI), totol
..,/1
-_..----
Pot... ha
(I( ). totol
../1
Surface Water
Total Metals sa.pling Re.ults
S.tenlum
(So), totol
..,/1
Silvor
(A,), toto I
../1
.----------
Ift.u"lcloftt SOMP'O or lotol Motol. Anolyol. not roquo.tod.
0.020 U ..81 0.011 O.OJO U
DAY
DI'
DU
DRY
DR'
DAY
DR'
DU
DRY
DRY
DRY
VALUE QUALifiERS. HA - An.lyto not roportod U - Anol,.od but not dot octo'
J - Pro.ont bolow dotoctlon 11.lt I - 'ro.oftt In I.borotorr bloft'
DAIA VAl IDAIION QUALfIEAS. (No voildo'ion quoll,tor Indlc.to. d.t. ho. not boon volldotod.)
Sodl- Strofttt- '''ol1t- Itn Vuodf-
(No). totol (Sr). toto I (n). toto I (Sft), Jotol (V). toto I
../1 ../1 ../1 ../1 ../1
M.. 1.25 O. Joo U NA 0.010 U
. . HoI"ftl ,,- ftot _t 1 . I.,,-to. voluo
M . lotch 0,1'0 ftot In 8O.12~ ron,o
A . AoJoctod, A. Accoptoblo .It" quoll'lc.tlon.;
" . "oltd
~
-------
STATION 63
St.tion
N...ber
$V-on
$V-on
$V-OIl
$V-OIl
$V-on
$V-OIl
$V-OIl
$V-061
$V-06J
$V-on
$V-06 J
$V-061
SW-061
0.'.
5..pl.d
07/24/87
07/0./88
01/28/8'
05/12/8'
0'/21/8'
07/19/89
08/11/8'
09/15/89
10/Ot/89
11/01/89
12/01/..
° 1/05/90
02/02/90
Surface Water
Total Metals S..pling Results
Zinc
(Zn). '0,.1
../1
---------
I...uftlel...,
0.020 U
DAY
DAY
DAY
DAY
DAY
DAY
OAY
OAY
DAY
DAY
OAY
5--.18 or '0,.1 "-,.1. A...lr.l. not reque.ted.
VALU£ QUALlfIEAS: HA. Anelr'. not reported U . Anelr.ed but ..ot detected
J . Pr...ftt ~..ow ..tectton I..it . . .r...nt 1ft '."retlr, ~1.n.
DAIA VALIDA I ION QUAI flEAS: ("0 v.lldetlon qu.llfler Indlce'e. det. h.. not bee.. velldete..)
. . 118ldl... tI- ..ot -t ( . htl_t.. veh.e
N . 'etch .,I.e ..et I.. IO-iloa re..,e
A . .eJeetedi A. Accept,"e with qu.llflcetlo....
"'
v . "elld
-------
STATION '4
Stet ton
NU8ber
SW-064
SW-O"
SW-O"
SW-064
SW-064
SW-064
SW- 064
SW-064
SW - 064
SW-064
SW-064
SW-064
SW-064
O.t.
h..l.d
--.------
07/22/.7
07/07/88
OJ/JO/89
05/U/"
06/27/"
07/"'89
0"11/89
0"20/89
10/04/"
1110'1"
12/01/"
01/05/'0
02/02/'0
. ,
Surface Water
Total Ketals S..pling Results
AIUMtnu. A""-,,y' Ar..nte hrt- I.r)' I 11- C...I- C.lcI- C..I- Chr_l-
(AI). toto I (5~). tot. I (Ao). tot.' (h). to,"1 (I.). to,"1 (Cd). totol (Co). to,"1 (Co). to,"1 (Cr). to.. 1
"'9/1 ..'I ..'I ..,1 ..,1 ..,1 ..,1 ..,1 ..II
--.-------- ----.-
Inlufflcteftt S.--1~ or 'ot., ~t.l. An81ya', Rot r.,y..ted.
0.IlOO U 0.006 O~I.I
15.4
DRY
_446
..,.
DAY
DAY
DAY
DAY
DAY
DAY
DAY
DAY
"
"
.0600 U A
.0600 U A
.0100 U "
.0100 U R
.200 U V
.100 U V
VALU[ OUALlfl[RS: HR. A"ol)'to "ot roport.. U - A"ol)'o.d byt "ot .otoct..
J - 'r....' below detection ".ft . . Pr....' 1ft 1.~.r.t.r, ~,.ft'
DAIA "ALIDAIION OUALfl[AS: (Ho volldot'o" qyol"lor '"dlcot.o do.. h.. "ot bo." vol'..t...)
0.002 U
.00SO U "
.0050 U V
0.007
.0050 U .
.0050 U "
6'.50
71.60
1M
"
. - 1to1.... tt- not _t I - Io"-t" v.l..o
N - lotch .".0 ".t ,,, eo-12ft ron,o
. . AoJ.ctod; A - Acc.,t.bl. .'th qy.II'lcotlo"o,
V - Volt.
IU A
. 100 U It
.,
NR
0.041
.0100 U A
.0100 U .
-------
STATION 6.
St.. ton
N_er
$W-M4
$W-M4
$W-O"
$W-O"
$W-M4
SII-O"
SII.O..
SII.O"
$W.064
$W.064
$W.O"
511.064
SII-O"
De'.
Sooopiod
-..---
01/22/81
01/01/88
0)/30/81
OS/22/81
06/21/81
01/11/81
08/11/81
01/20/81
10/04/81
11/01/81
12/oi/8I
01/05/10
02/02/'0
Cobolt
(Co). toto I
...1 I
"..uUlelont
0.020 U
ORY
.0500 U V
.0500 U V
DAY
ORY
DAY
DAY
DAY
DAY
DAY
DAY
Copper
(Cu). toto'
...1' .
Surface Water
Total Metals Sa8plinq Results
Iron
(fo). totol
.../1
Lood
('b). toto 1
.../1
So.,'o or Totol Hotol. Anoly.l. not roquo.tod.
0.041 11. I 0.004 U
.0250 U A
.0250 U V
.120
1.01
.0050 U A
.00110 U A
V
A
VALUE QUALifiERS: HA. An.lyto not roportod U . An.ly,od but not ..toe to'
J . Pr...,,' ".'ow .etact'oft It_tt I - 'r...n' tI, '....r.torr .'8"k
DAtA VAlIDA'ION QUALfIEAS: (No volldotlon qu.llflor Indlcoto. d.to h.. not boon volld.to'.)
Llthl-
(Lt). totol
.../1
Molno.I-
(...). toto 1
.../1
HR
56.1
.0125 A
.100 U V
44.80
n.lo
...",."....
(...). toto 1
.../1
0.H8
V
.0515
.0141
'"
Mercurr
(HI). toto 1
.../1
0.0002 U
v
V
.0002 U V
.0002 U V
. . IIoI"nl tt- not _t [ . [.tt-t04 volue
N . lotch ""0 not In 1O-11Oa ron,o
A . AOJoetodl A. Aeco,to~10 .Ith quollflcotlon'l
V . VoUd
~
Molp"on-
(Mo). totol
../1
NA
.0100 U A
-------
STATION 64
Statton 0.1.
NUMbor So..lod
$V-064
$V-064
$V-064
SW-064
$V- 064
$V - 064
$V- 064
$V-064
$V-064
$V - 064
SW-064
SW-064
SW-064
.-.----
01122/81
01107/88
0)/)0/89
0'!>/22/89
0"21/89
01/19/89
08/11189
0"20/89
10/04/89
11/09/89
12/01/89
01/05/90
02/02/90
-,
surface Water
Total Metals saapling Results
Nlchl 'ote..l- Set.ntw. StI"or Sodl- Strontt- 'holll- 1101 '0..0.1-
(HI), toto I (II ). tohl (So), tohl (A,). tohl (No). totol (Sr). totol (TI), toto I (501), Toto' (' ). toh'
.,/1 ..I' ""I ""II' ""III ""II' ""II' ..I' ..I'
-..-.------- ------..- --- --
In.ufflclont SeMplo Dr lotol Hotol. A..o'V.t. ..ot roquo.to..
3.'2 0.010 U 0.030 U
0.02J
DA'
.0400 U A
.0400 U ,
OA'
DA'
DA'
OA'
OA'
DAY
OA'
OA'
IIU ,
IIU A
.0115 V
.0050 U A
.0100 U V
.0100 U A
VALUE QUAL If lEAS: HA - An.I,to not roportod U - An.I"od but ..ot dot octo'
J - 'ro.ont bolow .otoctlon 11.lt . - Pro....t In '."rotor, blo..'
OAIA VALIDA I ION QUAL flEAS: (Ho "olldotlo.. quollflor Indlcoto. dote ho. not boon ..01 I do to..)
110
0.)00 U
NA
I. )1
101
11.)0
1.14
1.20
.0400 U A
.0100 U A
. 100 U A
. 100 U ,
V
V
A
. - HoI.I.., tI- not _t I - l.tI_to. ..oluo
N - 'otch 0,1'0 not In BO-IZaI ro..,o
R - AoJocto'; II - Accopt.blo with quo'ifleotion.; ,- Volld
-------
Stetlon O.t.
STATION 64
HU8ber
$V-ou
$V-OU
$V-OU
$V- OU
$V-064
$V-OU
SW-OU
$V-OU
$V-OU
$V-064
SW-OU
$V.064
$V-OU
So....l.d
.--.----
07/22/87
07/07/88
01/10/8'
OS/22/8'
06/17/8'
07/19/89
08/11/89
09/10/8'
10/04/89
11/09/89
11/01/89
01/05/90
01/01/90
Surface Water
Total Metals sa.plinq Results
ltnc
(In). tote I
../1
.--- ------
In.u"lcl.nt 5.....1. or Total Hotol. Ano',olo not roqu.ot.d.
0.111
OAY
.0100 U A
.077' V
OAY
OAY
OAY
OAY
OAY
DRY
OAY
OAY
VALUE QUALifiERS: "R - Anolrto not r.portad U - Anolr.ad ~ut not ..tact..
J . Pr.'.At "'0. 4etectton .t.tt . . 'r...ft' 1ft '.bere'.r, "8"'
DAIA VALIDAII~ QUALfIER5: ("0 vall.atlon quol"I.r Indlcato. do'o hoo not bo.n voll.ot.d.)
. - 1101.'''1 tI- not _t ( - (O"_'M ..oTua
" - latch 0,1.. "0' I" 10-110& ro"..
R - AoJ.ctod; A - Acc.ptoh'a wIt. quo""cotlono,
t
V . Volt.
-------
STATION
St.tton Date
H~or So~lod
SW-IOJ
SW-IOJ
5\I-IOJ
5\I-IOJ
5\I-IOJ
5\I-IOJ
5\I-IOJ
5\1- 10J
5\I-IOJ
5\I-IOJ
5\I-IOJ
5\1- 10J
5\I-IOJ
07/11/88
OJ/21/II
05/25/8.
06/15/11
071 U/89
08/02189
09/07/89
10/0J/89
II/OJ/89
12/06/89
01/18/90
02/12/90
OJ/22/90
Surface Water
Total Metals s.-pling Results
103
AI_ln- A"tl-"" Ar..nte "rl- lor,,11 1- Co..l- Calc 1- C..I- Chr-I-
(AI), toUI (Sb), totol (Ao), totol Clo), totol (10), total (Cd), toU I CCa), toto' CCo), toto' CCr). totol
-fill ..I' ' ..II ..I' ..I' ..I' ..I' ..I' ..I'
------ ---- -.--- ---
0.766 0.500 V 0.002 V 0.174 0.002 V 0.004 V ".0 ItA 0.020 V
119 V .0100 V A .0441 A 4.21 V .0214 A .0241 V 10) ( 1.11 V .172 '
Oa'a not ret rec.lved
2.11 V .0600 V " .OJII A .8)1 V .0050 V A .0050 V A 279 V IV V .0170 A
14.JO V .0100 V " .010J " .441 V . 0050 V V .0050 V V 208 V IV V .0100 V A
25.10 " . 0600 V V .0149 V .711 V .0050 V V .0050 U V 2M V IU V .0211 A
0.,. not yet received
2.60 v .500 U Y .oozo V Y .215 Y .0020 V Y .0040 U Y 109 Y .0010 U Y .0200 U V
Oat. not yet receIved
o.U not ,ot recelvld
DaU not ,ot recelvad
Oltl not "ot received
DaU not ,ot rocotvod
. . Ho'"'''' tt- not _t ( . (att_tool "a'uo
M . latcll ap"o not I" 80- U,", rOll'o
A . AoJoctod; A - Accaptab'o .Itll ~ua'lflcatlona;
V"LUE QUALlfIEAS, HA - Anal,to not raportod U - "nal)'zod but not "at octo"
J - Pr...nt b.lo. detect 10ft 't.lt 8 . Pr"'At 1ft ','.ratar, bl.R'
DAIA YAIIDAIION QUAlfIEAS, (Ho "alldatlon qu.llflor Indlcato. d.ta h.. not boo" "a"datod.)
V - Valid
..
-------
\.
....
surtace Water
Total Metals
saapling Re.ults
STATION 103
5ht Ion Doh Colla It I Copper Iron lo'" Lttll'- "",nu'- ",,"'0"000 ""rcur)' "'1)''''0''-
H_er 50..,10" (Co). tote I (Cu), 'otol (Fe). tohl (Plio). totol (L'). totol (HI), totol (MIl). 'otol (He). tohl (Me). to'ol
.,/1 ../1 ../1 ../1 ../1 ../1 ../1 ../1 ../1
------ -------
SV-IOJ 07/11/88 0.020 U 0.020 U 0.691 0.001 NIl 11.0 0.011 0.0002 U HIt
SV-IOJ OJ/2I/.. .224 " .21:1 . IU . .... " .... " ".eo V 10.70 " HA ."4 "
$V-IOI 05/1S/1t 00'0 ..ot rot racat"...
$V-10:1 06/11/11 .0500 U " ."" " 40.70 " .116 " .100 U " 5U V 1.18 " .0001 " .100 U "
511.101 07/1:1/" .0500 U " .0:116 V 11.70 " .0241 " .100 U " 15.70 V .... V .0001 U . .100 U "
$V-10:1 08/02/.. .0500 U " .0.,. " n.lo A .101 " .100 U " 18.10 " loll V .0002 U V .100 U V
$V-IOI 0'/07/" Doh not rot racetv84
SV-IOI 10/OJ/" . 0200 U " .0200 U " 2.88 " .0071 V .0110 " ".90 V .18. V .0002 U " .500 U "
SV-IOI II/OJ/" Doh not rot rec.tved
$V-IOJ 12/"/8' Doh not rot reeetvad
511-101 01/18/'0 Doh not )l'ot recetved
511-10:1 02/12/'0 Ooto not )l'ot recetvad
$V-IOI 0:1/22/10 Ooto not )l'ot racetvad
""lU[ QUAllfl[A5: HA - ""ol)l'to "ot roporto" U - ""01)1"0" lIu' not "otoctoll
J . 'r...ftt b.low detect.o" It..t . - Pr...nt In '.'.ratorr "on.
OAIA "ALIDA I ION QUAlflfAS: (Ho yolldotlo" quollflor I"dlcoto. doto ho. not boo" voltdoto",)
. . HoI...", tI- not _t I . loti_toil voluo
H . lotcll 0,1'0 not I" eo-IIGa ro.,o
A . AoJoctodl ". "ccoptolllo .Itll ~uo'I'lcotlo.o;
-------
.;.\
Burface Water
Total Ketals sa.pliDg Re.ults
STATION 103
5t.tlon O.te Hlc'" Pot...h.. Sele"'",
H_or SO",'Od (HI). lohl (I( ). 10101 (So). loh I
.9/1 ../1 , "'9/1
.......-.-- .------ --------
SW-IO) 01/11/88 0.020 U 0.128 0.005 U
SW-IO) 0)/2J/81 .21) A U.10 A .0250 U A
SW-IO) OS/25/81 Oe'e not re' received
SW-IO) 06/15/81 .0400 U A 5U A .0050 U A
Slol-IO) 01/1J/8I .0400 U A 5U A .0050 U A
SW-IO) 08/02/81 .0400 U V 1.52 A .0050 U A
Slol-IO) 01/01/81 Doh nol '01 recetved
SW-IO) 10/OJ/81 .0200 U Y 1.0) A .0020 U Y
SW-Io) 11/0)/81 Do" nol '0' received
Slol-IO) 12/06/81 00.0 not ,ot rocolvod
Slol-IO) 01/18/10 Do.. not '0' rec.lved
Slol-IO) 02/12/10 Dat. not ret rece'ved
SW-IO) OJ/22/IO Doh nol '0' received
S'lvor Sod'- SIronl.- '''011.- TIn Vonolll'-
(A,). tohl (No). totol (Sr). toh I (n). tohl ($nl. '0101 (V). totol
-./1 -./1 ../1 -./1 ../1 ../1
----- --- --
0.0)0 U II.) 0.)81 0.)00 U HA 0.010 U
.0100 U A 20.60 A 2.21 A .0100 U A .100 U A .UI A
.0100 U A 5U A IU A .0400 U A .100 U A .IIJ II
.0100 U A 11.)0 V IU A .0100 U V .100 U A .0504 V
.0100 U A ".10 V IU V .0100 U A .100 U Y .0tOt II
.OJOO U Y 12.10 Y .4)1 V .00)0 U Y IU Y .0100 U Y
YIILU[ QUIILlfl£AS: HA - IInol,.o no. ropor.od U . Anol,~od but not dotoctod
J . Pr...nt belo. deteettoft It.lt . . Pre.-nt In '.~or.tor, .'.n.
OAIA VALIDAIION QUALfl[AS. ("0 vol 11110' Ion quoll"or Indlcoto. do.o "0. nol boon vol'lIIo'od.1
. . Holdtn, tt- not -t [ . h.l_tod "oluo
N . 'otc" ""0 no. In 10-1201 ron,o
A - R_Jected; A - Accep'..,. with ~u.II'lc.tlon.;
Y . Vo"l1
f..
-------
STATION 103
Statton o.t.
Hu.bar Sa.plad
llnc
(bl. totel
"'1/1
..-..---
SW-IOJ 07/11/88 0.020 U
SV-IOJ OJ/n/II .772 A
SV-IOJ OS/25/11 0.'. not ,et rec.lved
SW-IOJ 06/15/11 .J24 A
SV-IOJ 01/1)/11 .111 V
SV-IOJ 08/02/11 .251 A
SV-IOJ 0'J/07/8'J 0.'. not yet received
SV-IOJ 10/OJ/8'I .0200 A
SW-IOJ II/OJ/8'J. 0... not ,et rec.t"ed
SW-IOJ 1l/0./8'I Date lOot rat rec.'ved
SV.IO) 01/18/'10 Oa.a "ot ,.t racelved
SW-IOJ 02/1l/'J0 0.'. not rat rac.lved
SW-IO) OJ/22/'O 0.'. not ya' received
Surface Water
Total Ketals Sa.pling Results
VALU[ QUAllfl(AS: NA - A".'yt. not reported U . Ana'r..d but not detacted
J . Pra.ant balow d.t.ctlon 11.lt . - Pr..."t I.. la.orat.rr 'Ia"~
014114 VAL 10141 ION QUAlflfRS: (Ho validatIon quallfl.r Indlcata. data haa ..ot ba... valldat.d.1
. . Mo'.'". t'" not ..t I . (att..,.. v.tu.
N - 'atch apl~a "ot I.. 1O-12~ ra....
R - RaJ.ctad: A - Acc.pta'i. "Ith .uall'lcatlo"a;
\
V - valid
-------
-------
..
....
SU~ACE WATE~ 1NT'Eq)M REMEDIAl ACTION PlAN
ROC'('" ~..A~S ~..A>r, GOi.DE.., CO~OAAOC
.g&g ..,ra:> wal~.r.. apC>e"a.pgl
APPENDIX B-4
SURFACE WATER SAMPUNG RESULTS
TOTAL INOAGANIC COMPOUNDS
-------
'.,
Surface .ater
Total IDorgaDic 8aapliDg Results
'03-PAD AND LIP SITB
N'iret.. '0'"
St.ttOft D.'. H"rl'.-Hltrog.n C"'orld. 5...,.,. 01...,..04 S0"'" HCOJ-
H-.r 5.."... fIG/L ~/L "/L "/L .../L
..----.
SWOSO / / DR'
$11010 07/2'/87 4. II 119.0 21.1 1110 211
SW050 01/"/" 0.41 41.1 14.1 454 180
SWSO 0'/"/" IHSUff It I(H' S_U '011 I-GAHIC ANALYSIS
$VOSO 01/11/19 DR'
SIIOSO 05/10/19 DR'
SW050 01/27/19 0.07 V 22 A " " J80 V JIG V
SWSO 07/18/" 0.22 17 14 JIG 480
SWOSO 08/11/19 DR'
SWOSO 0'/12/19 DR'
SWOSO 10/01/8' OIl.
SWOSO ../OJ/19 DA'
SWOSO "/01/19 DR'
SWOSO 01/05/10 DA'
SWOSO 02/01/10 DA'
SWOSO OJ/17/1O Oil' .
SIlOS I 07/21/87 4.10 II.' 11.0 JJI U.
swoU Ol/U/" OA'
SV051 04/11/19 DR'
SWOSI 05/10/19 DA'
SWOSI 0'/" /19 ..8 V J2 A " " HO V 2tO V
SIlOS I 07/18/" OA'
SWOSI 0./../19 DR'
SWOSI 0'/"/8' DR'
SVOSI 10/01/.. Oil'
SWOSI ,,/OJ/.. Oil'
SII05I 11/01/.. OIl.
SW051 OI/OS/tO 011'
SWOSI 01/01/10 DR'
SWOSI 07/21 /87 0.20 U 21.5 n.J III ,.7
SIIOSI O./U/.. 0.72 11.0 '7.' Ial 118
Swon 01/11/.. 011'
swan 05/10/19 DR,
SWOSI 01/0'/" OIl.
SVOU 07/07/19 OA'
VALUf QUAL I'll 115, HII. An.'". n.' r.por'." U . An.',.." ~..t not ...tectod
J . Pro.ont ~o'" ..otoctton ".1' . - Pro.ont In '."rotor, ~,..,
DAtA VALIDAtiON QUAL'IIIIS, (Ho ...lldo'108 ...'t'lor Indlc.'.. ...t. .... not '00. vo'ld.t."..
. - Holdlnl It- .ot _t I - hlt-tod ...,..
" - "Ic~ .,1'0 n.t I. 8O-1~ ro...
. - ..J.cl04' A - Accopt.'10 .It. ....1I'lcotl..., V - V.'I"
,6
-------
',0,
'Of
Total
8urface Water
Inorqanic 8aaplinq
Resulta
,03-PAD AND LIP 8ITB
Metra'..
H,trlto-Hltrogo"
HG/l
Chlorldo
"!ill
5..lhto
MG/l
5..tlo"
H_er
o.to
S...lod
---_. -.-
'ohl
0".01... Soli..
Ma/l
IICOI -
Ma/l
swou oe/II/8. OIlY
swon 0./11/8. OIlY
SWon 10/08/8. OIlY
SWon 11/01/" OIlY
swon 11/01/" OIlY
511052 01/01/.0 OIlY
511052 01/01110 OIlY
swon OJ/"/IO OIlY
5110U 01/21/81 0,28 U.O n,1 4t1 III
SIIOn 01/21/81 IH5Uff IC IIH' SNtPU '011 I-GAlliC ANALYSIS
swoss 01/22/" 0.18 aD,1 ".4 700 454
511055 08/.,/1. J.. V 28 V II II 810 V JIG V
511055 OS/25/8. 2.1 II J5 V " " .50 II 170 "
5110U 08/28/8. 2.0 V 4Z " ., V 410 V UO V
5\10U 07 118/" 2.4 4. 120 180 100
SW055 08/1"1' I.' V 58 V II V '10 " UO V
SIIOU 0"20/81 5.1 " 120 V '1 " 710 II 110 "
SWOU 10/1"" 5.1 V 115 V 7t V 180 " 100 II
SIIOSS II 10'1" 1.7 V n V .. II 1'0 " 1M II
5110SS "/07/" 4.5 n 100 710 114
SWOSS 01/1./10 2,1 V 41 V 51 V UO " JlO V
SWOU OI/U/lO o.'e "0' W.' r.celve"
5110U OJ/15/1O Doh "ot ,ot rocotvo'
SliD 57 07/21/87 1.16 24.0 1.0 U 122 UI
SVOSP "/U/.. OIlY
SWOl7 04/17/81 OIlY
511051 05/10/8' OIlY
511051 01/0'/" OIlY
SilOS 1 07/07/8' OIlY
SilO 51 01/11/" OIlY
SW051 0./11/81 OIlY
SII051 10/04/81 OIlY
SIIOS7 11/01/81 OIlY
SliD 51 12/01/81 OIlY
SliD 51 01/01/10 DAY
V"lUE QUAllfIEAS: HA - IInol,to "ot roport.. U - ""01,... ~..t "ot 'otocto'
J . 're.en' ..,.. ..tec"on II." I . 'r..."t .. '."reter, .,...
0"111 VllllDAIION QU"lfIEAS: (No v.II'otlo" ....II'Ior Indlcot.. d.to h.. "0' boo" v.II..to'.)
. . KoI.I", 'I.. "0' ..t I . 1.'1..,.. vol..o
. . lotc' .,1'0 "0' t. IO-IIGS r....
. - 'oJ.C'O'1 ,,- "cco,'.'lo .It' ...oll'lco.lo".. V - "oIl'
-------
",
surrace .ater
Total Inorganic 8a.pling Results
903-PAD AND LIP 8ITB
"Itrat.. ,...,
St.. ton De'. "l'rl'.-HI'ro,." Chlorld. 5..U.,. 0'...'''.. 50'1.. NeOJ -
"_or 58-.I.d Mr./l MG/l MG/L ",L "'L
---..- -----.------- ---
SIlO!>' 02/02"0 011'
51105' OJ,I1," 011'
SWOS. 01/21/81 1.42 ; J2.0 22.0 J11 IJO
$11058 O.,u,.. O.U II.' 11.1 411 J08
$11058 01'11'" 011'
$11058 05'10'.' 011'
511058 01/11'" 0.60 " JO " JO " 440 " JIO "
$11058 OJ,"'.' 011'
$11058 01'''''' 011'
$11058 0'/20'.' 011'
511058 '0/01'" 011'
511058 II/10'" 011'
$11051 12/0".' OIlY
SWlS8 01/05/10 011'
SWlS8 02'02/'0 011'
511011 06/22/88 0.10 U 55.J ".J "I J.
SIlO" OJ/JO/.. 011'
$110" 05/"'" 011'
$W011 0I/2J,.' 21 " ]I " " " '10 " no "
5110 11 OJ' ..,.. 011'
$WO" 01'''/'' 0.06 " JJ " 100 " 150 " 110 "
$W011 0'/20'.' 011'
$110 11 10'01/" 011'
5110 11 11/0./.. 011'
$W011 12'0"" 011'
5110 11 01/05/" 011'
5110 11 02'02'" DIIY
SII01J OJ, "'10 0... .... ..., received
"ALUI QUALIfIERS: "R. "".1..'. ..0' r.por'.. U . A".lr'.. ..., .... ..'.c'"
J . 'r.....' ..'0. ....c.'." 1..1. . - 'r.....' .. '...r...r, .,...,
DATA VAlIDATION QUAlfllA5, e"o ...'1..'10" ....I"'.r I"dlc,'.' d.'. h.. ..0' ..... ..1'..'''.)
. - Ho'.'" .... ..., ... I - I.....,.. ..,,,.
. - I.'c. .,1'. .... .. eo-IIGS r....
. - ..Jec'''1 A. "cc."..,. .... ...."f'c."Oft.' ,,- V.I'.
..
-------
'f
"
Total
Surface Water
Inorganic Sa.pling
Results
STATION 53
Hltrate. T.'.I
St.tton De'. HI'rl'.-HI'ro..n Chlorld. Sulfa'. OI...lv.' S.Itd. HCOI-
H_ar 5...1 ad "'/L "/L "'/L "/L "/L
--....----
SWOU 01/21/81 0.20 U 11.5 '0.1 ." 481
01/'1/. 0.10 u ' 10.' II.' IU I"
SWOU
swon 01/'1/. INSUffiCIENT SNtI'lI ,DA IHORIiAHIC -USIS
swot. 0'/05/" 0.11 " 61 " II " 860 " 860 "
swon 05/11/" 0.05 u A ,, " I U " 1'0 A UO "
swon 01/"/1' 0.07 " II " . " "0 " 710 "
swon 01/11/" DAY
swon 01/"'" 0.05 u " !i1 " II A 510 " 810 "
swoU 0"'0/" 0.05 u A 110 " It V 180 A 480 "
swon 10/12/11 0.05 U " " " 11 A "0 A UO A
swon II 101/1. 0.05 U " " " It A 520 A 170 "
swon 12/IS/" 0.05 u .1 U 500 85.
swon 01/11/10 08te no' Y.' rac.tvad
swon 02/11/10 0... no. Y.' r.c.lv.'
VALUE QUALIFIERS: HR - "n.I,to no' ro~rtod U - "nol,.o' ~ut no' 'o.oc'"
J - 'r..a.' "'ow ....ctlo. 11.1. I . 'r..o.t I. I."r.t.r, .1..'
DAIA ""LIDAIION QUALFIERS. (No ..II...lon qu.llflor Indtc.'.. d... h.. ftot ~a.. v.'I..t....
. . HoI.t.. tt.. fto' ... I . I.tt..,.. value
. . la'ch .,1'. not I. 1O-11Ga r....
-------
Surfaae Water
Total Inorganio Sa.pling Resulta
SOUTH WALNUT CRBBK
IIltre'.. '.h'
Station Oete Nltrlte-Hltrog.n Chlortd. . SuI"'. D'...'v.. 5.1'.. tlCOI-
N"".r S...'.d W./L ../L .../l IG/l ../l
-----.-.
SWOIII 07/2'/17 d.IO ad.O 71.' .77 148
SWON 01/10/.. 1.41 II.' 11.' 112 I"
SW051 Od/ n/', J.2 A 58 V II V ItO A 110 V
SW051 05/ II /.. 2.' A d5 V .1 V 170 A 110 V
SWOIII 01/07/.. J.' V 48 V 10 A 110 V 110 V
SWOII. 07/12/.. J.2 V " " .0 V 110 V 110 V
SW051 08/0'/" 2.' " II " 11 V 110 A 410 V
SWOSI 0'/ ../.. d.d " II A 41 " 180 A 110 V
SWOIII 10/ II/I. 1.1 " 17 V '0 " 71 A 100 A
SWOIII 11/11/" 2.' " " " rz V 110 A 120 A
SWOSI IZ./II/" J.I " II V II V 120 A 110 A
SWOS' OI/U/tO D.h "0' ,.. recetv.'
SWOSI 02/22/tO Do'o ... ,ot r.c.lwod
SWOSI OJ/" /10 Doh ..0' '0' received
5\1060 0,/21/.' d.1I U.O 11.0 182 ItO
SWDIO 11/11/81 IHSUfflCI£H' S_LI '011 INOIIGAN I C ANALYSIS
SWDIO O. /01/88 d.71 !II 12 d58 JOG
SWIIIO OJ/II/.. d.1 A 12 A II A 100 " 110 V
SWOtO OJ/II/.. 1.1 A 55 A 10 A 110 A liD V
SW060 05/11/.. J.I " dO V M A 120 A liD V
SWOtO 05/11/.. J.' " dO " dO A 120 A IdO V
$VOID 01/0'/" J.' " II V II V MD V 180 V
$VOIO 0./01/.' I.' V 50 V It V 410 A lID V
SWDIO 08/01/.. I.' V II V .. A UOD A JOG V
$VOID 0./11/.. 2.1 A n V 51 V 110 A ISO V
SWIIIO 0'/11/" 2.1 A IZ V II V. 110 A ISO V
SWOIO 10/0'/" I.J V 52 V II V UO A ISO V
$VOIO 11/01/" 1.5 V U V 41 V liD A ISO A
$VOIO n/OI/.' d.2 V II V U V 440 A Sto A
SWOIO 12/01/" d.' 50 41 liD 112
511010 01/21/'0 Do'o ..0' '0' roc.'ved
$VOIO 02/0./tO Do'o "0' ,ot r.c.lwod
SW060 01/12/tO Doh "0' r8t rec.lved
SW061 07/22/., 0.25 12.0 II.I 151 ".,
SWDII 11/11/17 IHSUfFIC I£H' S_LI fOIl INOIIGANIC ANALYSIS
V"lUE QUALlfIIRS: HR. ""0"'. "0' r.por'.. U . A...I,... 'U' .... ....ct"
J . 'r.....' "'OM ....c.'o.. "... . . 'r....' ,. '...r.t.r, "0.'
OAT" V"lIOAHOli QUAlfHRS. (Ho voll..tto.. ~uo'H'or I..dlc.'.. do" h.. .0' '8O. vo".o'''.)
. . "".1.. U- ..0' _t I . I.U.t.. ...Iu.
M . '.tc' .".. ROt I. 8O-11Ok r..,.
. . '.J.c'.., A. ACc.,'o". .t.. ~u.II'Icotl.".' V. V.I'.
,.
-------
. ,
\
...
Surface Water
Total Inorgan:ic Sa.pling a.sults
SOUTH WALNUT CRBBIt
"ftr.Ut 18,.1
Statton 0.,. "Itrtt.-HI'ro,... C"lorld. SIIIt.,. O'...lv.' Solt.. NeO) -
1I_.r So..I.d MG/l "/l HG/l "/l "'I.
.. -- ._-------
SWOII 07/01/88 4.6 50 II.' ... III
SWOII 01/20/11 I.' If 81 II 2t A II II "0 "
SWO'I 05/11/11 4.1 " U " 41 " JOG " "0 "
SWO'I 01/0'/11 4.1 V I' " 50 " no " 1'0 "
SVOII 01/01/" 5.' V 41 " II " 410 A 110 V
SVOII 01/01/11 1.1 V JI " II V 400 " JOG V
SVOII 0./11/11 4.0 " " " JO V 150 " 110 V
SVOII 10/01/11 1.8 V II " 50 V 410 " 280 V
SVOII 10/20/11 OR.,
SVOII 11/01/11 1.8 V 10 " 41 " 400 II no "
SVOII 11/01/" 1.6 J6 10 J80 JOG
SWO'I 01/21/10 Det. lIot ,.at rec.t.,..
SWO'I 02/0'/10 00'. ..0' J" roc. tv..
SWOII 01/11/10 0.,. ..01 J" r.u tv..
SVOII 01/11/10 0.'. "ot re' r8c81..4
SWIOI 01/10/88 0.1 U 1.:1 21 486 150
NIOI 01/11/11 0.0:1 U " ) U v I' " 110 II I' "
NIOI 0:1/ II/II 0.11 A I U " 14 " "0 " " "
SVIOI 01/01/" 0.01 " I " " " 12 V JJ "
SVIOI 07/11/11 0.0:1 U V I " " " II V 18 "
SWIOI 01/0'/" 0.05 u V I U " I' V ,. A II V
NIOI 0'/14/11 0.05 U V 20 " " ' 10 A II '
SVIOI 10/1./11 0.05 U " I " iii , "0 " II "
SVIOI 11/1:1/11 0.0:1 U V I U " It V II II . A
SVIOI 11/"/11 0.05 U A I U " " ' If " II "
NIOI 01/25/10 0.,. ..0' ...t rec.t...
SVIOI 02/22/10 00'. ..., J" roc.tv..
SWIOI 01/21/10 0.'. "ot ,et rec.tve"
'lIlU( QUAll'I(AS, NR - 11...1". ..0' r.,or'.d U - ,,".1,... bll' ..0' ....c...
J - 'r...... "I.. ..,.c.to.. II.tt . - 'r...... I.. I...r.t.r., .1..,
OAI" VAllDIIIION QUAl'I(AS: (110 v.II..tto.. qll.ltft.r t..dlc.t.. d.,. ".. "0' b... v.I".,...)
. . ",1.1... II.. ..., .., ( . 1.'1..... ".IMO
II . "tc.. .,11. ...t I. 8O-1~ r....
-------
Total
surfaae Water
Inorgania Sa.pling
Results
STATION 5'
"Uret.. 'oto'
51.a'on D.'. Hltrlto-Nltrolo" Chlorldo Sot.hh DI..olvo' 50.ld. tlCOI-
H_.r 50...10' f'fG,L "'" t MG,L ...,t "'L
---_.- -- -*---.-.
SWOII 07/21/87 1.80 ' 1'.0 24.1 124 UI
SW05. 07 '01'" I U U 4.1 114
SW051 01/20/" 4.4 " 41 " 18 " 110 " 100 II
SW051 05/11/" 2.7 " 27 II II " 110 " 410 II
swon 01/08/" 4.1 II 51 II II " 410 II 140 II
SWOII 07/01/" 4.2 II 4. II 51 II 520 " 100 II
SW05. 08/10/" 1.1 41 41 110 JIG
swon 01/18/" 4.1 v II V 10 " 110 " 410 V
SW051 10/01/" 1.1 v II V 41 V 210 " 400 V
swon II '01'" 4.2 V 41 V 41 V 410 " 170 "
swon 12/01/8. 4.2 50 41 480 Je4
swon 01/21/10 Dot. ..ot rot rece'v.d
SW051 02/0./10 Doh ..ot ,ot rece.v.d
SWOSI 01/12"0 D.h ..ot ,ot recetve"
V"Lu[ QUALifiERS: HA. "...Ir'o IIOt r.,ort.d U . "...Ir..d _Mt 110' ..toct..
J . 'r.....' _.1.. ..t.ctlo.. 11.lt . . 'r.....' I.. '.--r.t.r, -....,
D"I" V"LIDA'IOH QUAL'IEA5. (Ho v.'I'."o.. ,M."f'.r ,..dlc.'o. d.'. h.. ..0' _.... v."'.'ad.)
. . .....,.., tI- IIOt _t I . loti-tad MOh..
N . '.tc' .,1'. ...t I.. 10-1101 r..,.
. . ..J.C'." ". "cc.p,._I. .'t' ,u."f'c.t'...., II. V..,.
/
-------
..
..
Total
8urface Water
IDorgaDic ...pliDg
Results
8TATIO.. 63
M'tre'..
St.t'on 0.'. "ttrtto-Httro,o. Ch10r t..
"_er S...Io" t'fG/l ","/l
. "----_._---
IVon 01/24/" 0.20 u 10.5
SVHI 01/N/.. 0.1 u 51
SWO'I 01/28/11 OIlY
IVon 05/12/" OIlY
SIIon 01/28/11 OIlY
IVon 01/1'/11 OIlY
SIIOU 08/11/11 OIlY
IVOU 0'/15/11 OIlY
SIIOU 10/04/.. OIlY
5110.1 11/0./11 IIIIY
IVon 12/01/11 OIlY
SIIOU 01/05/'0 IIIIY
sIIon 02/02/'0 IIIIY
Sulfot.
Ma/L
'.tol
Dlooolvo. Soltd.
MA/l
HCOI-
M'l
111
II'
.15
151
HI
..
VAlUI QUAL If lIAS; HA. Anol,.o .0' rop.rt.. U . Anol,.o' ~. .ot ..otect..
J . Pr..o.t '.10. 'ot.etton It.tt . . Pr..ont tn 10~rot.~ ~I..'
DAIA VAllDAIION QUAlfllAS, ."0 y.lt....to. qu.ltftor t..te..o. ..... ~.. not ~... v.lt......)
. . HeI.t.. .t.. ... ..t [ . I.tt..t" v.I..
N . '.te' .pt.. ..t t. to-IIGS r..,.
-------
STATION 64
Hltreto.
St.tlon Ooto "Itr'to-Nltro,o.
H_or S..,'od r«>/l
SWO" 07/22/'7 0.20 U
SW084 07/07/" 0.2
SW084 01/10/11 '011'
SW084 OS/22/1. 0.011 U "
SW084 "/"/.. O. S7 ,
SWH4 07/1./.. 011'
SW084 01/11/.. 011'
SV044 0./20/.. 011'
SV044 10/04/.. 011'
SWH4 11/0./.. 011'
SWH4 12/01/" 011'
SWH4 01/011/.0 011'
$VOl 4 02/02/10 011'
Surfaoe .ater
Total Inorganio s..pling Results
'0'"
C"'orldo S.. Ifoto D'..olv.d So'id. tlCOI-
M/l ../L "/l "/l
41.1 11.0 HI 404
I 4.0 U 110 441
0.1 U
.. , UO " "0 " 110 v
II " 110 ' "0 ' 110 '
'''lUi QUAll'IIRS: ~. Afto"t. not roportod U . "n",.od ~..t .ot detoct..
~ . 'r...nt "I.. d.t.et'.. ".It . . 'ro.o.t ,. '...r.ter, "",
00\'" V"lIOo\tlON QUAl"I.', (Ho voUdot'o. "uUflor 'nd'cat.. dote "0. .ot "0.. v.U..t".)
. . ""d'.. tt- .ot _t I - IItt.'" v.'uo
. - I.'e" .,1'. ..t I, 10-1'" r....
. - "Joet.d, ". Acc..t.~,o .".. "u."f'cot'on.. ,. ,."d
t
-------
,
'.
4.
Total
Surfaae Water
IDorgaaia S88pliag
Results
STATION 103
MUr.',. ,.,.1
5'."on 0... M'.r".-M'.ro.." Chlor .... 5..1f.,. 'DI...lv." Sol'''. 1tC0I-
"""'.r 5_1... "'/L ../L "/L "/L M/l
SWIOI 01/11/88 II 40 II 147 III
SWIOI 01/11/" 1.1 A II A II A 110 A n. v
SWIOI 011/111/.. 1.1 A II V .. V 110 A .10 V
SWIOI 08/111/" 11.1 II I' II .. II 470 A NO V
SWIOI O'/U/.. 1.1 II JI II II V 00 " NO "
SWIOI 08/01/.. '.1 " 40 A II A 470 " 110 "
SWIOI 01/0'/" 5. I " II A III " 440 A JOG V
SWIOI 10/01/" 4.1 " .. " III " 110 A no "
SWIOI 11/01/.. 1.0 " 10 " III A 110 A 110 A
SWIOI az/OI/.. 1.1 J1 to ..0 III
SWIOI 01/1./10 0018 "., ,., roc,'v."
SWIOI Ol/az/IO 0018 .., ,., roc. Iv."
SWIOI OJ/U/IO 00.. ... ,., roc. Iv."
"ALu[ QUALI'IIAS: ~. A".I,.. "0' r.por'," U . A".I,.... .... "., .....c....
J - 'r...,,' "low ".'.c'I." I'." . . 'r...". I. '...r...r, .....
OA'A "ALIDA'ION QUAl'II'S. (Mo v.I'''...." ....I"'.r '''dlc.... d.t. -.. "0' ..." v.II"""'.)
. . NoI..I.. .... ".. ... I . I.....,... v.I".
M . ...c. .",. ".. ," 1O-11OS r....
-------
-------
~
-~
APPENDIX 8-5
SURFACE WATER SAMPUNG RESULTS
DISSOLVED RADIOCHEMISTRY
SURFACE WAiE~ INTE~Jt.1 REMEOIAl ACTION F>lAN
~KY FLoATS PLANT. GOLDEN. COI..OAADO
~;. "Irati ',...,nut .8Dpena.pgl
-------
" .
8urface ..ter
Dissolve4 Ra4iocheai.try Saapling R.sults
'03-PAD MfD LIP SITB
Statton 0... Grol' Alph. Gro.. I.t. S'rontl- 81, 10 'lutonlW8 2JI, 240 ""rlel- 241 Ir"'-
"_er 5....1.. ptt/I 00II. ,cl/I 00II. ,cl/' 00II. ,cl/I 00II. ,cl/' 00II. ,cl/' ....
-----..--- -------- ------.-..
SW050 / / OIlY
SWOIlO 07/21/17 ...
SWOSO ./17/88 5.11 ! J.II 5 '.II! 4.47 lilt 0.175 ! 0. J47 0.2 tit ..
SWO!lO 04/27/88
SW050 04/11/11 DAY
SW050 05/10/11 OIlY
SW050 ./17/11
SW050 07/18/11
SWOSO 01/11/11 OIlY
SW050 01/12/11 OIlY
SW050 10/04/11 OIlY
SW050 11/01/1. OIlY
SWOSO 12/01/11 DAY
SWOSO 01/05/10 DAY
SW050 02/01/10 DAY
SW050 01/11/10 DAY
SW051 07/21/17
SW051 ./n/II DAY
SW051 04/11/11 OIlY
SW051 05/10/11 OIlY
SWO!lI ./27/11
SW051 07/18/" DAY
SW051 01/11/11 OIlY
SW051 01/12/11 DAY
SW051 10/04/11 OIlY
SWOSI 11/01/11 DAY
SWOSI 12/01/11 OIlY
SW051 01/05/10 DAY
SW051 02/02/10 DAY
SW05Z 07/21/17
swon 04/n/88 0.174 ~ J.77 ' 0.00 ! 4.10 , lilt 0. H' ! 0.1'5 0.2 " ..
swosz 04/11/11 DAY
SW052 05/10/11 DAY
swosz 01/01/11 DAY
swosz 07/07/11 DAY
SW052 01/11/11 DAY
VALU[ QUALI'IEAS. tit - An.'~t. not r..u..'.. or .n.l~t. ..t. not ~.t r.e.lv..
... - 1..."lcl.nt S..,I. or '.41.c...t.tr~ A..I,... ..t r..ve.t...
OAf A VAllOAflON QUAl'IEAS, ("0 v.'I..tt.. 8w.'lfl.r tn.te.t.. ..t. ... n.t .... v."..ted.)
. . IoJectedl
A . Acc.,t..'. .1'. 8u."f'c.tt".1
" .'''.''4
If
.
-------
Surfaae Water
Dissolved Radiocb..istry sa.pling ..sult.
'03-PAD AND LIP 81TB
S..,lo" 0.'. 10..1 Uren''''''
"_er S...,.d ,et /' ....
------.-----
SW050 / / OIlY
SVOIO 01/211"
SW050 01/"/88 2.860
SV050 01/21/88
SV050 04/11/89 OIlY
SV050 05/10/89 OIlY
SW050 06/21/89
SW050 01/18/"
SV050 08/11/8' OIlY
SV050 0./12/89 OIlY
SV050 10/04/8' OIlY
swoao 11/01/11 OIlY
swoao 11/01/11 OIlY
SW050 01/05/10 OIlY
svoao 02/02/.0 OIlY
SV050 01/11/90 DRY
SVOSI 01/21/81
SVOSI 01/11/88 OIlY
SWOSI 04/11/8. OIlY
SV051 05/10/8. OIlY
SVOSI 06/21/8'
SWOSI 01/18/8' DAY
SWOSI 08/11/8. OIlY
SWOSI 0./82/8. OIlY
SVOSI 10/04/81 OIlY
SWOS I 11/01/81 OIlY
SVOSI 82/01/8' OIlY
SVOSI Ol/OS/IO OIlY
SVOSI 02/02/.0 OIlY
SVOSZ 01/21/81
SWOS2 01/21/88 1.120
SWOS2 04/11/8. OIlY
SVOS2 05/10/8. OIlY
SVOSZ 01/0./8. DAY
SVDS! 01/01/8' DRY
SVOl2 08/11/8. OIlY
VALUE QUALifiERS: HA - Anolyto not rl~YI.tld or ono'ytl ..t. not rot rlellvld
... - I".utrlct.nt S...,. or AI.U.ch..t.lrr A...,~... ..t r..u..'M.
DATA VALIDATION QUAl'IERS: (Ho v.lldotlol ~Yo'lfllr Indle.tl' d.,. ho. ftO' ,".ft v.I'..,"..)
. - "J.e'H.
A - Acel".". wI'. ~y.I"'e.'I..'1
~
.
-------
'O]-PAD AND LIP SITS
Dissolve4
St.. Ion 0.'.
Nun.r S...'ed
SW05Z 09/28/89
N052 10/0./..
SW05Z II/OJ/..
SW05Z 12/01/.'
svo5Z Ol/OS/'O
SW05Z 02/02/'0
SWOSZ OJ/I7/'O
SWOSS 07/ZI/.7
N055 0,/21/.,
N055 01/22/..
SW055 0./11/..
SW055 OS/251.'
SW055 01/28/8'
SWOSS 01/18/8'
SWOSS 08/11/8'
SW055 0'/20/.'
SWOSS 10/1'/8'
SWOSS 11/0'/8'
SWOSS 12/01/11
SWOS5 01/16/10
SW055 02/2)/'0
SW055 OJ/15/'0
SWOS7 01/21/87
SW051 01/2)/-
N051 04/11/.'
SWO!l1 O!l/IO/II
SW051 01/09/11
SWOS1 01/01/11
SW051 08/11189
SWOS1 0'/16/11
SWOS1 10/04/"
SWOS1 II/OJ/.'
SWOS1 12/01/89
SWOS7 01/05/'0
SWOS1 02/02/'0
SW051 OJ/I1/1O
Gro., A'ph. Grol. I.t.
pet/I .... pCt/1 ....
-----. ---- -- u_-- -. - --- ..-.
DAY
DA'
DA'
DA'
DAY
DAY
DA'
2.10 ~ 4.40 1 0.00 ! 5.01 9
0... ..ot ,ot r8c.tv8c8
DAY
DA'
DAY
DA'
DA'
DAY
DAY
DA'
DAY
DAY
DA'
DRY
DAY
..,
Surface Water
Ra4iocbe.istry sa.pling
Result.
Stron't- .'. 90
Pluto"f~ 2J9. 240
,Ct/I ....
pCt/'
....
----
--.--- .
1111
0.00 ~ 0.8"
VALUE QUAllfIIRS: 1111 . A...I,to not roquo.tod or .n.lrto d.lo not rot rocot.o'
... . I..u"felont S.."o or A..'oc~..'.trr A..'r.o. .ot roquo.to'.
OAIA VALIDAtiON QUAlfIIAS: Clio ..lld.tlon qu.llflor Indle.to. dot. ~o. not .00. .."'.t....
_rlcI- 2.1
. ,CI/I
l1li
II . .0Joe'0., A. Aceop'o.lo .'t. q.oll".o""o,
....
V . V.".
t
'rltl-
pC'/l
"'0
..
-------
Surface .ater
Dissolved Radiocbeaistry sa.pling Results
,03-PAD AND LIP SITB
Statton O.t.
H,ueber So...I.d
511052 0'/2./8'
5W052 10/04/.1
SWOS2 11/01/.1
511052 12/01/.'
511052 01/05/10
5110U 02/02/'0
511052 OJ/11/IO
511055 01/21/81
511055 0,/',/.'
SW055 01/22/88
511055 04/11/.1
5110SS OS/25/.1
5110SS 06/2./81
5110SS 01/1./.1
511055 08/11/.1
511055 0'/20/.'
511055 10/1'/.'
SIIOSS 11/0'/.1
511055 12/01/.1
511055 01/11/'0
511055 02/21/10
5110SS 01/15/90
511051 01/21/81
511051 01/11/88
511051 01/11/.1
511051 05/10/.'
511051 01/01/.1
511051 07/07/.1
511051 08/11/.'
511051 01/11/81
511051 10/04/.1
511051 11/01/.1
511057 12/01/.1
511051 01/05/90
511051 02/02/90
511057 OJ/I1/90
101.1 UrenluM
pCI/1
oed.
--.. --------
OIlY
OIlY
OIlY
DAY
OIlY
OIlY
OIlY
$.020
0... not ret recetved
OIlY
OIlY
OIlY
OIlY
OIlY
DAY
OIlY
OIlY
OIlY
DAY
DAY
DAY
DAY
VALUE QUALIfiERS: "A . Aft.lr" no' r.qu....d or .n.lr'o .... no' r.' roc.'.o.
... - IR..fftct.nt S.-pl. or A.~t.ch..'.trr Aft.',... ..t r.~u..t...
DAIA VALIDATION QUAL' lEAS: (No ..I'd,"on qu"",.r 'nd'c.'.. d... h.. .0' .... ..1".....)
R - RoJ.c.o., A. Acc.,...I. w"h qu,""c"""I
~
V - V....
-------
Dissolved
Surfac. .ater
Radiocbe.istry Sa.pling
R.sulta
'G3-PAD AIfD LIP SITB
Statton 0... GrOll Alph.
N-er S...I.d pet/I ....
-..._--
5\IOS8 01/21/81
SWOS8 06/"/88 0.141.:).1J .
SVDSI 04/11/.. 011'
5\IOS8 05/10/.. 011'
5\IOS8 01/21/..
_SI 01/14'" 011'
SVOS8 08/11/.. 011'
SWOS8 0'/20/" 011'
SVOS8 10/04/" 011'
SVOS8 11/20/.. Oil'
SV051 12/01/.. 011'
5\IOSI Ol/OS/" 011'
SVOSI 02/02/" 011'
SWO 11 06/12/88 5.11 .: 4." 1 O.OD .: 5.11 ' NI 0.0215 lO.1U NI NIl
SV011 01/)0/" Oil'
SV011 05/11/" 011'
5\1011 01/21/..
S\l011 01/"/" 01'
S\l011 08/ ../.,
5\10 11 0"20/" 01'
$\1011 10/04/" 011'
SW011 11/0'/" 011'
5\1011 12/01/" 011'
5\1011 01/05/'0 011'
5\1011 01/02/'0 01'
$\1011 OJ/../"
Grol, ..,.
,£t/I
Md.
Str..tt.. I'. "
,£t,1 ....
Plutont.. 2).. 240
,et/I ....
Mortct- 24.
pCl'l
....
IrUt-
,e1,1
....
..._--~u_--
----
----.-----.-.. -.--
0.00 .: 4.80
8
NI
1.01 .: 0.)60
0.2
NIl
NIl
VALUE QUALI'I(IIS, NIl - An.I,t. not r..u..t.' or .n.I,t. '.t. not ,.t r.C.lv.'
... - Ift'~"tct.ft' I...,. or .....c.....tr, ...1,... ... r~_..t...
DAIA VALIDAIION QUAL'I(AS, (No v.lt..tton .u.I"t.r tn.tC.t.. '.t. ~.. not b... v.lt..t...t
. - ..J.ct.., A - Acc.pt.bl. wit. .u.II'lc.tt...,
v - V.U'
"
-------
Dissolved
,03-PAD AIfD LIP SITS
St..ton 0.'. 10181 U,.ntum
"_or 5..,Iod ,CI,I ....
--,-----_...
SIlOS. 01/'11/'1
SII058 "/21'" 4.'00
SIlOS. 04/11'" 011'
SIlOS. 05'10/" 011'
51105. 0&/'1'/"
51105. 01/'4'" on
SIlOS. 0"11/" 011'
SIlOS. 0"'10/" 01'
SIlOS. 10/04'" 01'
SIlOS. II /'10'" 011'
SIlOS. 1'1/0 I /.. 01'
SIlOS' 0./05/10 01'
SII058 0'/0'1/'0 011'
5>1011 0&/"/" 4.160
SIlO 11 01/10'" DAY
SIlO 11 05/11/.. 011'
SIlO 11 0&/'11/..
5\10 11 01/11/.. 011'
$\1011 0" ../..
5110 11 0"'10'" 011'
SIlO 11 10/04/" 011'
5\1011 II '0"" 011'
511011 1'1'01/" 011'
511011 01'05'" 01'
5110" 0'1/0'1'" 01'
5110 11 0)/"/'0
Surface Water
aadtocb..tstry S..pling
VAtu[ QUAllfl[A5: NR - Anolrto not ro,uo.'od or onol"o dot. not r.' roeoluod
... - In,urflelon' S..,lo or Rodloe.._to,r, An."'.. "0' r~u..'".
DA'A VAllDAIION QUAl'I[RS. ("0 v.lld.tlon ,uo.I'lo, Indl..'o. d.'o "0. 00' ~o... uo.ldo'od.)
a.sult.
. - "Joe'"1 A - Aeeo,'o~lo ..,~ ~uol"'eo"".1
Y - V.lld
-------
Dissolved
Surface .ater
Radiocb..istry sa.pling
Results
STATION 53
Stltton V.U 6ro81 '''ph.
HY8II.r 5...1.. pCI/1 Old.
-.. -.------.-
SW051 01/21/87 ... I
swan M/II/" ..4. ~ 4.14 .
swan M/II/..
swan 04/05/81 2 ~ 6
swon OS/211.'
swau M/21/.' ...
svou 01/1'1.' DAY
swa5J 08/151.'
svou 0"20'.'
swou 10/12/.'
swon 11/011.'
swou 12/15/.'
$W05J 01/11/90
swou 02/U/'0
-.-..--- - --.-- ---
Plutonl- 2)9. 240 _rlcl- 241 Irlt'-
pC./1 .... pC./1 .... ,CI/I ....
---....-.--
1.89 ~ 0.851 0.7 NIl ..
0.20 ~ 0.01 0.01 ~ 0.01 MIl
GrOI' I.'.
pCl11
.....
Stront'- .'. 90
pC'/' ....
0.15J~5.15
,
""
1 ~ 4
0.0 ~ 0.4
VAIU[ QUAII'IERS. NIl - An.l,t. not r.qu..t.d or .n.l,t. d.t. not ,.t r.c,'v.d
... . 1..."lc'.nt 5..,'e or R...loch..l.tr, An. I,... .et requ..t...
DAIA VAIIDAIION QUAI'IIRS. eNo v.l.d.t'on qu.I"'er In"c.t.. ..t. h.. not ,... ..,...t...)
. . .eJecte'l A. Acc.pt.". w.th qu.l.f'cet....,
v . V."..
-------
Dissolved
Surface Water
Ra4iocheaistry S..pling
STATION 53
5...lon
Nuebar
D..-
5...,1..
lot.1 Ur8nh-
pCI/1
Old.
--...----------
$\IOSJ 01/21/"
$\IOU M/U/.. 1.260
$\IOU OI/U/88
SW05J 04/05/11 2.000
swon OS/2J/II
swon 01/21/..
SW05J 01/1./.. OA'
$\IOs) 01/15/..
$\IOU 0./20/11
$W05J 10/12/11
$\IOS J 11/01/11
SWOU 12/15/11
SWOSJ 01/11/90
SWOSJ 02/1J/90
VALUE QUAll'IIAS; HA . An8'rte not raqu8.ted or 8fte','e de'. not ,et rec.tve4
... . IRlufftclan' S..". or ..4toc...t..r, Afta'"., ne' r..u..'.'.
OAIA VAIIDAIION QUAI'IIAS, (No v.lld.'lo. .u.II'I.r 1..1..,.. d.,. ~.. .0' .... v.II..,...)
. . .'Ject'dl
A - A...p,.bl. .I'~ ...11'1..'1....
Result.
v . V.It.
-------
surface Water
Dissolve4 Ra4ioche.istry sa.pling Resulta
SOUTH WALNUT CREEK
Stetton o.to GrOll Alph. Gro.. I.'. S'ron'lY8 .,. 10 'Iy'oniUM 219. 240 _rlclY8 241 tritiUM
"_er So... I od p(t/I lOCI. pCI/' ..... pCl/' .... ,CI/' .... pCI/' .... pCI/' ....
. - ------- ...----..----- ------- ._---
SW056 01/21/81
SWO!18 "/JO/88 1.21 !. 4.15 I 4.84 !. 4.66 ... 0.00 ~ 0.126 0.] HA ...
SUOSI 04/U/" 2!. . I ~ 1 0.1 !. 0.1 0.00 ~ 0.01 -0.02 ~ 0.01 ..
5101051 05/11/11
SW056 06/01/11
$W051 01/12/11
$WOSI 08/01/11
SU051 09/14/11
$WOSI 10/1./11
5101056 II/III/II
$W051 1Z/1I/89
NOSI 01/25/10
$WOSI 02/22/10
51oIOS6 ol/'il/IO
511060 01/21/81.
SW060 11/11/.,
$W060 01/01/88 1.64 !. 1.88 I U.2 !. 4.9. 7 Ita 0.00 ~ 0.0851 0.2 HI NR
$W060 OJ/II/II 7 !. . 2 ~ 4 0.1 !. 0.1 0.02 !. 0.01 0.00 ~ 0.01 Ita
$W060 01/11/.' 4 ~ 7 I ~ 4 -O.I~O.. 0.02 ~ 0.01 -0.01 ~ 0.01 Ita
SUOIO 05/11/.'
$W060 05/15/.9
SU060 06/01/.'
$W060 07/01/11
$W060 01/01/11
SW60 09/11/11
$W060 09/11/.'
SUOIO 10/OJ/8'
SWNO 11/08/8.
$W060 II/OIl/II
$W060 1Z/06/11
$W060 01/21/'0
$W060 02/09/10
$WOIO 01/12/10
$W061 07/22/87
SW061 11/11/11
SWOII 07/01/88 20.6!. 5.74 6 41.7 ~ 1.44 7 .. 0.108 ~ O.IU 0.1 NR NR
VALUE QUALlfl[RS. HA . An.'rto not roquo.'.d or ...'rto d.'. not rot r.colvo'
... . In.u"Iclo.' 5."'0 or ...loch..I.'rr An.tr.o. no' ro,u..'o'.
DAIA VALIDAIIOM QUALfIERS. ("0 v."'.'Io. ,u.'I'lor In'I..t.. d.'. h.. .0' ...n w.tt..,...)
I . .0J.ct.'1
A . A..op,..I. wl'h ,u.II'lc.'lon.1
, . ,.It.
-------
Dissolved
SOUTH WALNUT CRBBK
Station Dlte lot. I Urent"'"
N_er Sa.. 10. ,et/I ....
o ._--~-----
5\1OU 01/21/81
SV05. M/M/.. 1.0'0
SV05. Ol/U/" '.100
SW05. 05/../81
SV05. 0./01/81
S\IO 5. 01/12/"
SilOS. 01/0'/"
SilOS. 0./11/81
SilOS. 10111/81
swon 11/15/81
SW05. 12/1./81
SW05. 01/25/.0
SilOS. 02/22/.0
SW05. 01/21/'0
511060 01/21/81
SWO'O 11/11/11
5110.0 01/01/88 10.210
5WOIO 01/11/" 1.100
SW080 01/1./81 5.200
511010 05/15/81
511080 05/15/"
5W080 0./0./"
SWOIO 01/N/"
5W080 01/01/..
SWOIO 0'/11/"
SWOIO 0./11/81
5\1010 10/01/"
SVOIO II/N/"
511010 II/N/8I
5110.0 Il/N/"
SW080 01/21/.0
5WOIO 02/0./.0
5WOIO 01/12/.0
SilO II 01/22/81
SWOII 11/11/11
5WOI I 01/01/88 '.110
Surraae Water
Radiocbe.istry Sa.pling
YALU[ QUALlfIER5: NI . An.I"o no' ro,y..,o. or .n.I". ..'0 no' '0' rocotvo.
... . ,..."tc'.n' s...,. or R..'.c_"'.'r, An.',... .0' r.,y..,o..
DAIA YAllOAllON QUAlfIIAS. ("0 v.lt.."on qu.ll,t.r In.'c.'.. ..,. -.. no' .... v..t..,...)
. . 'OJ.ct..1
A . Acc.,'..'. .1" ,y."f'c."".1
Result.
v . V.It.
-------
80UTH WALNUT CRBBK
Dissolved
8urface .ater
Rad!ocbe.istry 8a.pling
Results
5..'lon D...
M......r 50..lod
5WII 01/20/81
SWOII 05/18/"
SWOII 01/0'/1'
511011 01/M/"
511061 Ol/OJ/"
511011 01/11/"
5WII 10/OJ/"
511011 10/20/"
SWOII 11/01/"
511011 It/M/"
5WII 01/21/10
5WII 02/0'/"
SWOII OJ/12/1O
5WOII 01/12/10
511101 06PO/II
511101 06/ U/"
SWIOI 05/11/"
SWIOI 06/01/"
511101 01/12/"
511101 01/0'/1'
511101 01/16/"
511101 10/11/"
511101 11/15/"
511101 12/1'/"
511101 01/25/10
511101 02/22/"
511101 OJ/21/IO
Grol, Alpho Grol. 10" Stro"U- ". '0 "..to..l- 211. 260 _rlcl- 261 'rtt 1-
,[1/1 ""0 pCI/1 !lido pCI'1 8do ,(1/1 "'0 pCI/1 "'0 pCI/1 "'0
------- -- --- ----- ...----.-- ---.----- ---.-.------
6 ~ 6 1 ~ J -0.2 l 0.6 0.01 ~ 0.01 0.00 l 0.02' ItA
011.
0.00 ~ 2.62
° l I
..12 l 6.01
I ~ 2
HI
0.2 ~ 0.6
0.00 l 0.M61 0.1
0.00 l 0.01
6
VAIU£ QUAllfl£A5. HI - A"ol,to "ot roq...otod or o"ol,t. do'o ..ot ,.t roc.lvo'
... . Iftlw"fe'.n' S...,. or ...toc-....tr, AR"".' fte' r.~u..'...
DAIA VAIIDAIION QUAI' If AS. (Ho volld.tlo" ...oll'lor 1..'lcot.o 'oto hoo ..01 '0." voll.ot...)
HA
-0.01 : O.OJ
HI
HI
I . 10Jocto.,
A - Acco,to"o with q..olt'lcotlo"OI
v - Volt.
-------
8urfaaa .ater
Dissolve4 R.4ioabe.i.try 8..pliDq Re.ult.
80UTH WALNUT CRBBK
St.tton Det.
Nu".r S,,,'"d
SW061 OJ/20/8.
_I 05/11/11
SWOI. 01/0./11
SWOI. 01/01/8.
SWOI. DB/OJ/B.
SW061 01/11/11
SW061 10/OJ/1l
SWOI' 10/20/11
SWOII 11/01/8.
SWOII 1l/0I/8.
SWOII 01/2J/.O
SWOII 02/01/.0
SW06' OJ/12/1O
SW061 OJ/12/1O
511101 06/)0188
SWIOI oe/u/.,
511101 05/11/8.
SWIOI 0./01/8.
SWIOI 01/1l/8.
SIIIOI 08/0"81
SWIOI 0./14/8.
SIIIOI 10/18/8'
SWIOI 11/15/8.
SWIOI Il/II/II
511101 Ol/U/.O
SIIIOI 02/22/.0
SWIOI OJ/2I/'o
10'.' Ur.ntuM
pCl/1
Old.
2.500
DAY
0.611
0.200
VAlU[ QUAllfl[AS: HA . An..,tl nl' rl~uI.tld or .n..,tl d,'" not ,.t rlcllvl'
... - Iftlulf'e'.n' S...,. or A.d'oc~..'.trr Aft.'~... "8' r.~y..t...
DAIA VAIIDA'ION QUAl'lfAS: (No v..ld.tlon qu.'lfllr Indlc,'", d.,. ~.. no' b.l. v..I'.,",.)
. - .IJoe,...,
A . Acc.,t.... wl'~ qu.II'lcI'I...,
,
v - VIII'
-------
Dissolved
STATION 59
Shllon 00'. Gro.. A I ph.
H_er 50..lod pC'/' lOdo
----..- . - ..
SWOIII 07/21/81
$WOII 01101/.. II.OJ ~ '.06 1
swon OJ/20/81 "~12
$VOSI 011/11/81
SWOIII 01/08/81
SWOIII 01/011"
$VOIII 08/10/"
5WOIII 01/18/"
5W051 10/OJ/"
5W051 "'Ol'"
swon 12/01/..
SWOSI Ol/U/1O
$VOSI 02/01/10
$VOIII OJ/12/1O
Gro'l I.'a
pe:'/'
- ---'---'..--.-'-
'.2' ~ '.87
. -. i I
"".
Surface water
Radiocbe.istry sa.pling
Result.
lOde
Str..ttM8 II. 10
pC'" lOde
Plutonl- 2J1. 240
,et/, ...
-----
.---
H.
-0.' i 0.'
0.0111 ~ 0.0621 0.07
0.01 ~ 0.01
'AlUf QUAllflfRS: HR - An.ly'. not r.~u.otod .r .n.lyt. ..,. no' y.' r.c.lv..
... . 'A.wl'lct.nt S..,I. or ...'oc,....trr A..I.... fte' r.,y..'e4.
~I" VAII~'ION QUAl'lfRS: (Ho v."d.t'o. ~u.II".r 'ndlc.t.. ..t. h.. not ,... .o,t.oted..
Aooorlc'M8 .11
pCt/'
1Od.
-
-0.01 i 0.0'
. - 'oJocto.1 II - Acc.,t.'I. wIt. ~uo'tflcotl..ol
v . Vo""
,
Tr'tt-
pC'/'
...
..
..
-------
Dissolved
STATION 59
St.tlon o.t. Tot.1 Ur.ntU8
Nu.b8r ,..., lod ,CI/' OIdo
--- .------
SW05. 07/21/87
SVD5. 07/01/.. 5.660
SW05. 01/20/11 7.500
SWOSt 05/11/11
SWOSt 01/08/"
SW05. 07/01/8.
SW05. 08/10/11
SWOSt DI/18/11
NOS' 10/01/..
SW5. 11/01/81
NOS' 12/01/81
NOS' 01/21/10
swon 02/0./10
51105. 01/12/10
Surface Water
Radiocb..istry sa.pling
VAlU£ QUAll'I£AS: NA . Ano'r'o no' requo.'04 or ono'r'o 40'0 no' rot rocolv"
... . 1..u"lc'.n' ,...". or A04'.c~"'0'rr A.olr.o. ... req..o'...
DArA VAlIDA,rON QUAl,r£AS, (No v.'ldo"on ~uo"".r 'n4'co'0. 40'0 ~o. .0' .... vO"40'.4.)
Result.
A - A.J.e'''1 A - Ace.,'o". ~,.. ~.o"f'eo""ol
,
...-
-------
Dissolved
8urfaae Water
Radiooh..istry 8a.pling
Result.
STATION 63
.-.--_.._--
----------
PlutonlU8 2J.. 240 MerlclU8 241 Irltl-
,el/I .... ,el/I .... ,el/. ...
----_.--
0.07S0 l 0.0871 0.07 ItA ..
Stetton
"~.r
0.'.
5.,.1..
Gro.. A1ph.
,Ct/I
....
Gro.. I.t.
,el/I
....
S.r..tIYO ... 10
,ell I ....
_II 07/24/17
swon 07/01/11 I.IS l 4.72 I 18.' l S.I2 8 NIl
SWOII OJ/28/.. OIlY
SWOl I OS/12/.' OIlY
SW06J 01/21/" OIlY
SW06 I 07/1./11 OIlY
SWOII 08/11/11 OIlY
SWOII O./IS,II OIlY
swon 10/04'" OIlY
swon 11/01/11 OIlY
_n 12/01'" oRY
swon OI/OS/tO DAY
SWOII 02/02/tO OIlY
VAlU( QUAllfIEIS. HI . A..lrto .0' roqu..'o~ or ...Irt. ,.t. not r.t r.c.lu.1
... . I..uf.lcl.nt S.,.I. .r '.~I8C~..I.tr, A..I,... n.. ro.u..t.~.
DAIA VAllDAIION QUAlfIIAS. ("0 ..lld..to. qu.llflor Inllc.'.. I... ~.. no' bo.. ..It~.'ol.)
. . '.~8Ct.~1 A. Acc.pt.~I. .It. qu.llflc..I".1
" . ".II~
.
-------
Dissolved
STATIOR 63
5,.,'on Vet. lot.1 Ur.nt...
H"'.r S....'.d ,et/. M.
---"---
NOU 07/2./.7
SW08J 07/N/ee 17 . 7.0
SW08 J OJ/28/.. DAY
SV06 J 05/1'/.' 011'
SW06J 0./21/.. 011'
NOU 07/11/" 011'
SWOU 08/11/" DA'
S-J 0./15/.. 011'
NOli) a%./.. 011'
NOU II /OJ/.. 011'
NOU 12/01/.. DAY
swoe J Oa/05/1O DAY
NOli) 02/0'/'0 DAY
Surface water
Radioobe.istry Sa.pling
YALUI QUALlfIIRS. HR . An.'". n.' r.,u..'.' .r .n.','. ..,. n.' ,., r.c.'w.'
... . I..uffle'.n' s--... .r ..".ch,,'..r, A..',... ... r.......'.
DAfA VALIDAflOH QUAL'IrAS, (No walt...tton ,u.''''.r 'n"eata. ..... ".. no' .... .............)
Result.
. . "Jac''''a A. Ace.,'.h'. ...h ~.1'f'C."".,
,
..-
-------
Dissolved
STATION ,.
Stetton De'. 6,.0.. A'ph.
"_or So..,lod pCl/1 OIdo
_n___..
5\1064 07/22/87
swe6 07/07/88 6.36 ~ 4.31 .
SW064 03/30/81 011'
SW064 OS/22181
SV064 06/27/"
SWOU 07/11/.. DR'
5\1064 08/11/" DAY
SV064 01/20/81 DA'
SWOU 10/04/81 DA'
swe4 II /0'/" DAY
SWO.4 12/01/.. DA'
5\1064 01/05/.0 DAY
SVO.4 02/02/10 DAY
6,..0" I.,.
pCI/1
------------
7.20 ~ 5.U
Surface Water
Radiocbe.istry S..pling
Results
OIdo
S'ro.'IY8 .', 80
,CI'1 "'0
'lu'o.l~ 231, 240
pCl'l OIdo
--------
8
H-
0.00 ~ 0.201
0.3
YALUE QUALlfIIRS. HA - Anol"o no' ro~uo.'od or onol"o d.,. no' '0' roeoluod
... . 1...IIlelon' S..,I. or R.dloe~..I.'rr A..I,... .., r.~uo.'...
~IA VALI~JION QUAL' lIAS: (No ..lld.'lon ~uollll.r I.dle.'o. d.,. ~.. .0' .... ..I,..'.d.t
IIooorlelY8 141
pCt'l
OIdo
IIA
- . "Joe'.dl A. Aeeop,.bI0 wl'~ ~uollfle.'t"'1
v - V.lld
.
IrltlY8
pCl'l
....
ItA
-------
Dissolved
STATION 64
Statton
"_.r
O.te
5...'.d
'ot.1 Ur.ntu.
,CI/'
....
----
SW064 07/22/11
SW064 07/07/N IS.UO
SW06 4 OJ/JO/.. DAY
SW06 4 OS/22/8'
SW064 0'/"/88
SW064 07/1./88 DAY
SW064 08/11/.. OIY
SW06 4 0./20/.. DAY
SWOI4 10/01/" OIY
SW064 11/0./.. OIY
SW061 12/01/.. OIY
SW06 4 01/05/80 DAY
SW061 01/02/80 OIY
Surface Water
Radiocb..istry Sa.pling
VAlU[ QUAllfl[R5: HR - An."t. not r.~Y.lt.d or Inl"t. d.t. not ,.t r.e.lv.d
... - I.....fftct...t ...." '1' ....tech....,,.., ""..,... .., r.......'84I.
OAf A VALIDAIION QUALfI[AS: ("0 v.ltd.".. ~y.1I ft.r Indle.t.. d.'. "II .., .... ...'''1.'". J
Results
. - ..JoC'edl A - Acc."..I. wi'" ~..'lflc.'I""1
. - .01ld
-------
STATION 103
Station
""..r
SWIOJ
SWIOJ
SWIOJ
SWIOI
SWIOI
SWIOI
SWIOJ
SWIOJ
511101
51110J
SWIOI
SWIOI
SWIOI
De'.
58.,...d
01/11/88
OJ/n/..
05/15/8.
06/15/8.
01/U/..
08/0l/8.
01/07/8'
10/01/8'
II/OJ/..
IZ /01/..
01/18/10
Ol/Il/IO
OJ/22/.0
. ,
Surface Water
Dissolved Radiocheaistry Sa.pling Re.ult.
Gro.. A .,h.
,cl/I
Gro.. I.t.
pet/I
SIro.ttw. .,, 10
pCI'I ....
Plulo.tu. lJ', 240
,ct,1 ....
....
Old.
---- - ..-... ----
'--'-.----
-----
-----.
..OJ : ..U
II ~ .
10
21.1 ~ 10.2
-4 ~ 4
20
l1li
-0.2 ~ 0.4
0.00 ~ 0.0877 0.1
0.01 ~ O.Ol
YALU[ QUALlfl[AS: NA . A..lrl. .01 r.qu..'.. or ...Ir'. d.'. nol r.' r.c.lv..
... . I..ufflcl..' S..,I. or I..toc...'.trr A..lr... .0' r.....tad.
DAfA YAllDAflON QUALfl[AS: (No v.II..tlo. qu.ltfl.r I.dlc.to. d.'. h.. .0' .... .."..t.4.)
AIoortctw. 241
,c','
....
..
0.00 ! 0.02
I . aoJoC'.d. A. Acc.,'..I. wt,. qu.I'ftc.tt...1
v . V.It.
frlt tw.
,ct"
lid.
!III
HI
-------
Dissolved
STATIO. 103
Stetlon O.t. lot.. Ur.,.,,,
Nueber 5...I.d pC'/1 1Od.
------------
SVIOI 01/11/88 1.440
SWIOI 01/11/" 1.100
SVIOI OS/25/"
511101 01/11/"
SVIOI 01/11/"
SVIOI 08/0'/"
511101 0'/01/"
511101 10/01/"
SVIOI 11/01/"
SVIOI 11/01/"
511101 OI/I./tO
SVI OJ OZ/I~/tO
511101 OI/U/tO
Surface Water
Radioche.i8try Sa.pling
VALUE QUALIflEI5, HI . An.I,.. no. ro~u..'.. or .n.I,.o .... no' ,.. roco'v..
... . ,.."U'cl.n' 1..,1. .r 1..locll_htr, Aul,... n.' r.~_.'".
DATA VALIDATION QUAL'IEA5, (No v.I'..,'on ~u.I'f'.r 'n.'c..o. ..'0 II.. no' .... v.I'..'".)
Re8ult.
. . I.Joe'", A. Accop...I. .".. ~..I'f'c."...1
II . Vo".
-------
-------
J
APPENDIX B-6
SURFACE WATER SAMPUNG RESULTS
TOTAL RADIOCHEMISTRY
S;;I<~ACE WA'rE1< 1Nr'E1
-------
Surface Water
Total Ra4ioche.istry s_pling Results
903-PAD AIID LIP SITE
Stet Ion Ooto Groa. Alpho Gro.. Iota Stro"th. .'.10 ""tonl- 231 _rlet- 241 'rttt-
N...or SI..,lld pCtli lOdo pCtli ""0 pCt/l .... pCt/i "'" pCtli "'" pCt/i "'0
----- -----
SWIIO / / 011'
SW50 07/21/.7 211 ~ 14 I' ~ III cl.O 115 ! 7 0.0 ~ 27 cUO
SVOIIO "/27/" HI NI HI 0.121 ! O. U. 0.08 HI III ~ »27 100
SVOIIO 06/27/.. Ooto "ot ~.t. reC8 t wed
SVOIIO 04/17/" 011'
svoso 05/10/.. DIY
SVOSO 011/27/.. JZ ! . 7 24 ! 5 0.7 ! 0.5 O. J.4!0.1 0. O. 71 ~ 0.01 O. 20 ! 220 II
SVOIIO 07/11/" Olto not yo' rec.'ved
SVOSO 01/ "/" DIY
SWOSO 0./12/.. 011'
SVOSO 10/04/" 011'
svoso .. /OJ/.. 01'
svoso 12/01/.' 01'
SVOIIO 01/05/.0 DIY
SVOSO 01/01/.0 oA'
SWOSO OJ/17/.0 OA'
SVOIII 07/11/.7 Y! 4 ,. ~. cl U! J 0.0 ~ U cUO
SW51 oll/n/.. 011'
SVOIII 04/17/" 011'
SVOIII 05/10/" 011'
SVOIII 011/17/.. II ! J J u! a J 0.0 ~ 0.4 0. 0." ! 0.04 0. I.O!O.I 0. -120 l 110 II
SVOIII 07/1./" DIY
SVOSI 01/11/.' 011'
SWOSI 0'/11/" DR'
SWOSI 10/04/" DIY
SVOSI ,,/OJ/" DR'
SVOSI "/01/8' 011'
SVOIII 01/05/10 OA'
SWOSI 01/02/10 OA'
SWOS2 07/11/.7 114 ~ 10 411 ! III cl 1.4! 1.5 0.1 ! 1.5 CliO
svosa "/23/" HA HA fill 0.11'5 ! 0.11. 0.1 HI 0.00 In. 100
swon 04/ J7 /8. DIY
SWOIII 05/10/.. 011'
SVOIII "/0./.. DR'
svosa 07/07/8. oA'
SV052 08/11/8' oA'
VALUE QUALlfIEAS: HI - Anol,to not rlquootod or Inolrto dotl not ,ot roeotvod
... . 'RIMIftee.n' S...I. or Aedtoch..t,trr Aftl"'.' Rot requ..'.4.
DATA VALIOAIION QUAlfIEAS: (Ho volldotlon quoll,tor Indteltol dote hll not boo" v.lldotod.)
. . .0Joetod;
A . lIeeoptoblo .Ith qu"It'le"tlo,,",
V . Villd
-------
Total
Surface Water
Radioche.istry saaplinq
903-PAD AND LIP SITB
Stetton Oe'. Tot.' Ur.ntu,"
H_Ir SI....lld pC111 Mdl
SVOSO 1 1 DAY
SVOSO 07121/87 2.120
SVOSO 06/27188 2.640
SVOSO 06/21/88 08'. not '.'. roc.lv.d
SVOSO 04/17/8. DAY
SVOSO 05/10/81 DAY
SVOSO 06/2718. 4.500
SWOSO 07/18/89 D.'. not ,e' r.cetv8d
SWOSO 08/11/81 DAY
SVOSO 0"12/89 DAY
SWOSO 10/°4/8. DAY
SWOSO II/OJ/8. DAY
SVOSO 12/°1/8. DAY
SVOSO 01/°5/.0 DAY
swoso 02/°21.0 DAY
SWOSO 0]/17/.0 DAY
511051 07/21/87 1.200
SVOSI 06/'''88 DAY
SVOSI 04/17/11 DAY
SVOSI 05/10/89 DAY
SVOSI 06/27189 2.600
SVOSI 07/11/8. DAY
SWOSI 08/11181 DAY
SVOSI 0"12/11 DAY
SWOSI 10/04/11 DAY
SVOSI 11/01/11 DAY
SWOSI 12/01111 DAY
SWOSI 01/05/.0 DAY
511051 021021.0 DAY
SWOS2 07/21/87 I. 770
SVOS2 061"/18 J. 710
SVOS2 04117/11 DAY
SVOS' 05/10/89 DAY
SWOS' 06/0"11 DAY
SWOS2 07/07/89 DAY
SVOS, 08/111" DAY
VALUE QUALlfIEAS: HA . An.I". no' r.qu.I'.d or Inol". dot. not ,., r.c.lvod
... . Inlufflclont S.-plo or Aodtoch..tltr, AnI1,... no' roqul.tod.
DATA VALIDATION QUAL flEAS, ("0 vllldltlo" qUlllflor Indlclto. dlt. h.. not be.. w.ltd.tod.)
. - "Joet"1
Result.
A . Acclpt..I. .tt~ qu.ltflc.tl'.'1
;
..
-------
surfaae Water
Total Ra4ioaheaistry SaaplinCJ Results
SOUTH WALNUT CRBBK
S'.'Ion D... Groll A1ph. Gro.. I.'. Stre.."- 1',10 Pluton 1- 2)1 Merlcl- 241 'rl"-
N_ber S...led pet/I -.I. pCI/1 -.I. tlCl/' .... pCl/1 .... pCl / I .... pClI' "'e
----... ---. ---
SWSI 07/21/" I .: 10 "1 II 3.1 0.0 .: .11 0.0 .: 2.0 <110
SWII 01/30/" NA NA NA 0.170 ! 0.110 0.1 Nil 0.00 ! )12 500
SWOSI Ol/U/" II .: 21 22 .: I 0.3 ! 0.1 0.20 ! 0.03 0.10 ! 0.01 110 ..: 1110
SWOSI 05/"/" U1 17 31 .: 10 -0.1 ! 0.1 0.11,: 0.02 0.01 1 0.02 lOG ! 1110
SWOSI 01/07/" 200 ! !l0 ,. i II 0.310.1 2.510.1 0.10 ! O.O!l 110 ..: 220
SWSI 01/12/" " .: !I 21 U,: 1 10 0.2 !, 0.4 O. 0.05 !, 0.01 O. 0.01 ..: 0.01 O. 110 1 110 21
SWSI 01/0'/" 0... not "et rece'v.d
SWOSI 0./11/.. 0.1,: 2.0 II 5 10 .: 3 A I 0.' 10.. 0.1 0.00' i 0.001 0.00) 0.005 i 0.001 0.001 -IlOO !, 100 lOG
SWOSI 10/11/" O.t. not r-et received
SWOSI "/15/" Oet. not "et received
SWOSI 12/ ../.. De.. ..ot Ifet received
SWSI 01/25/.0 De'. ..ot "et received
swOSI 02/22/.0 De.. ..0' Ifet rec.tved
SWOSI 01/21/.0 De'. no' Ifet recelv.d
SW060 01/21/87 I .: II U.:24 <1.0 O.O!,l.l O.O!, 1.2 <110
SWOIO 11/"/1'
SWOIO 0'/01/" NA NA NA 0.115 .: 0.141 0.09 NA 0.00 ..: U5 IlOO
SW060 03/16/.. 1 .: I 3 i I -0.2 ..: 0.' 0.02 .: 0.01 0.01 ! 0.02 JO ..: 1!l0
SWOIO 01/11/.. 1 ! I 214 -0.1..: 0.1 0.03 !, 0.02 0.02 ..: 0.02 170 ..: 110
SW60 05/15/" 2 .: 5 1 .: 1 -0.1 ! 0.1 0.04 ..: 0.02 0.00 ..: 0.01 JOG ..: 210
SW060 O!l/I!I/" 4 ! 5 7 .: 1 -0.1 ..: 0.1 0.00 .: 0.01 0.00 ..: 0.01 150 ..: 210
SW060 01/01/.. 14!,1 I .: 1 0.0 ..: 0.4 0.02 .: 0.01 0.02 !, 0.01 110 ..: ISO
SW60 01/01/.. '1 J 1 .: 2 0.0 1 0.4 0.01 .: 0.02 0.01 !, 0.02 -10 ..: 110
SWOIO 01/01/1. 0... not "et recetved
SW60 01/"/" 1.01 .1 .1 7.5 .: 2.1 2.8 -.01 .: .31 .11 .0121 .012 .OU Nil 100 1 220 310
SW060 01/11'" NA NA .24 ! .18 ... . 001 .: .001 .007 .011 ..: .012 .010 140 ..: no 170
SWIO 10/03/.. 0." not "et receive"
SW060 "/01/" 0... ..ot Ifet recelv.d
SWOIO "/01/" D... ..0' Ifet received
SWOIO 12/01/.. 0... no' ret recet".d
SWOIO 01/21/10 o.t. not ret received
SW060 02/01/.0 D." not "et recel"ed
SW060 01/12/.0 0... not re' recelv.d
SW061 01/22/., 11 1.2 ".: II <1.0 0.0 ! .12 0.0 ..: 1.2 <110
SWll 11/11/.,
SW61 07/01/.. NA Nil Nil 0.0654 1 0.0115 0.07 NIl 0.00 ..: )11 IlOO
VALU[ QUALlfllAS, Nil - A...I"te not reque.ted or .n.I,,'e d.t. not ".t rec.lved
... - I..~f'tct.ftt S...,. or ...toch..t,trr Anl'r'.' RDt r..M..t84.
O.'A VALIDAIION QUAlfllAS, (No v.lld.tto.. queltfter tndlc.'.. d.'. h.. not bee. v.ltd.t...)
II - II.Jectetl.
A . Acc.pt."le .tt~ que'lflc.tt.....
v - Ve1td
.
-------
Total
Surfaoe .ater
Ra4ioobe.istry Sa.pling
SOUTH WALNUT CRBBIt
Statton 00'0 10'0' Urantu..
H...bar So.,. '.41 pCI/1 1Od.
SW051 07/21/87 3.]90
SW051 01/30/88 ...70
5\/051 04/1)/8. 5.000
5\/056 05/11/8' 7.200
5\/051 06/07/8. 10.600
5\/051 07/12/8' '.000
5\/051 08/0./89 DoU no' ,.., rec.lved
5\/056 0./14/89 8.090
5\/051 10/18/89 0.'. no. ,at rac.t".d
5\/056 11/15/89 DoU n.' ,., roeo'..od
5\/056 12/1./89 OoU no' '0' r.e."'."
5'1051 Ol/U/'O OoU no' ,., rac.t"."
5\/05' 02/22/.0 Oat. "ot ,.., recee".d
5\/056 03/21/.0 Oau no' ,., race tv."
SW060 07/21/87 4.270
5\/060 11/11/87
5\/060 07/01/88 10.570
5\/010 03/1'/89 '.400
5\/060 03/18/89 8.600
5\/060 OS/15/89 3.200
5\/060. 05/15/89 3.300
5\/060 06/0./89 5.000
5\/060 07/00/.. 5.800
5\/060 08/03/89 0.'. not ~.t rec.t".'
5\/060 0./11/89 2.170
5\/060 09/11/89 3.J70
SWOIO 10/03/89 Det. not yat racetved
SWOIO 11/00/89 DoU no' ,., r.e.I..."
SW060 11/00/" DoU no' ,., roc. I.....
5\/060 12/00/.. OoU no' ,et recetve'-
SW060 Ol/U/.O Oat. not ,., recat"a.
SW060 02/09/90 Oat. not ,., racatved
5\/060 03/12/90 O.U no' ,., racatyad
SW061 07/22/87 1."0
SWOII 11/11/87
5\/011 07/01/88 9.]90
VALUE QUAllfl(AS: HA . An.,,.t. not ro~w..'." or .n.tr'. d.,. no' r.' r.e.I..."
... . Inoufflet.n' S..,t. or A...toe~..I.tr, An.tr... no' ro~y..t.".
DAtA VAIIDAIIOH QUAlfIlAS: (Ho ..."...tton ~y."fl.r Indlu'.. d.U ~.. not b..n "."",'ed.)
II - II.J.e'edl
Result.
A . Aee.p,.'t. .1'- ~y.'tfle.'t.n.1
,
...
-------
Surface Water
Total Racliocbe.istry S..pliDCJ Results
SOUTH WALNUT CRBEK
Station o.t. Gro.. A1ph8 Gro'l '.'a Stro..tl- ",'0 P'uto..l- IJ. _rlcl- 141 Trltl-
H-.r 5.."." pCl/' oncI. pC'/' Md. pCl/' Md. pCt/' Mdo , pCl/' Mdo pCt/' Md.
-----
SW061 OJ/IO/8. . ! 5 6 ! J -0.4 ! 0.4 0.04 ~ 0.01 0.03 ~ 0.02. -'0 ~ 110
SW061 05/18/.. 6 ~ 1 . ~ 3 -0.3 1 0.6 0.01 1 0.01 0.01 1 0.01 JOG 1 110
SW061 0./0./.. II ~ 1 U ~ 3 0.1~0.3 0.01 ~ 0.01 0.01 ~ 0.03 -30 1 no
SW061 07/0./.. 6 ~ 3 1 ! I -0.1 ~ 0.4 0.02 ~ 0.01 0.01 1 0.01 -10 1 140
SW061 O./OJ/.. O.to not )'.t'recelved
SW061 0./11/.. 4.. ! .' .7 '.61'.1 1.5 .1It 1 ... ..4 .00' ~ .006 0 HA 280 1 140 J80
SW061 10/OJ/8. Ooto not yot rocoh,o"
SW061 10/20/8. OIlY
SW061 11/06/8' 00 to ..ot yot roco"'o"
SW061 82/06/.' Ooto ..ot yo. rocol"o"
SW061 OI/U/90 00 to ..ot yo. rocol"o"
SW061 01/0./.0 Ooto ..ot yot rocol"o"
SW061 03/82/.0 00'0 not yot rocol"o"
SW061 03/11/.0 0.', ...ot yo. recelwed
SWIOI 06/)0/88 HA HA NIl 0.046J ! 0.116 0.2 HA 0.00 1 302 600
SWIOI 04/ U/.' 190 ! 70 140 1 JO 0.6 ~ 0.' 0.17 ~ 0.04 O.H ~ 0.10 30!1!I0
SWIOI 05/11/.. 780 ! 110 570 1 100 1.1 ~ 0.' J.J 1 0.1 0." 1 0.01 180 1 110
SWIOI 06/07/89 170 1 50 110 1 '0 0.' 1 0.' 0.71 1°.04 0.17 1 0.06 .0 1 210
SWIOI 07/12/.. " ~ 10 10 21 1 5 0"10.7 O. 0.37 1°.03 O. 0.00 ~ 0.01 O. -10 1 no II
SWIOI 08/0./.. 0.,. not yot rocol"o"
SWIOI 0./ ../8. -0.41 0.8 . 0.. .. 1 2 A I 0.071 O.U 0.5 0.002 1 0.004 0.006 0.006 1 0.001 0.01 -JOG 1 300 400
SWIOI 10/1./.. O.to not rot rocol"o"
SWIOI 11/15/89 Ooto ..ot rot rocol"o"
SWIOI 82/1./89 00 to not rot rocol"o"
SWIOI 01/25/.0 Ooto ..ot rot rocol"o.
SWIOI 01/22/.0 Ooto not rot roco"'o"
SWIOI 03/21/90 Ooto not yot roco"'o.
VALUE QUALlflEAS, HA . Ano'rto ..0' ro.uo.to" or .nolrto ".t. not yot rocot"o"
... - In..f,tc'.nt S8..1. or A.dtoc~..t.trr A""'r'.' Rot requ..t.d.
DATA VALIOAIION QUALfIEAS: (Ho "oll..tto.. quoltflor In"lc.to. "... ho. not boo.. "o'I"oto..)
. . .0Jocto.. A. Accopto"o .tth .uo'tflco.to....
V . Voll"
.
-------
Surface Water
Total Ra4iocbe.istry S..pling Results
SOUTH WALNUT CRBBK
Stet'on o.t. lot., Uranium
HU8ber S....lod pet/' ...to
-- - -_u o____n-
SW1161 03/20/89 2.~00
SW06I 05/15/8. 4.800
SW06I 06/0./8. 5.800
SW1151 07/06/89 5.600
SW1161 08/03/89 Dote not r.t 'rec.lved
SWIll I 0./11/8. ~.060
SWIll I 10/03/8. O.t. not ,at racelvad
SWIll I 10/2°/8' DA'
SW1161 11/0./8. Dote not rot recetvad
SWIll I 12/0./8. Dote no' ro' recel..e.
SVOII OI/U/90 Dote no' re' recetve.
SWII6I 02/0./.0 Do'o "0' ret recet".d
SWOII 03/12/90 Dote no' Je' racetvad
SW061 03/12/90 Dote ..ot ro' rec.t"e"
5\1101 06/30/88 2.188
SWIOI 04/U/19 4.100
SWIOI 05/11/89 6.800
SWIOI 06/01/8. 2.000
SWIOI 07/12/8' 2.200
SWIOI 08/0'/89 Do'o not rot rec.tved
SWIOI 0./14/89 II .100
SWIOI 10/18/8. O.t. "ot ,at racafyad
5\1101 11/15/8. Dote no' Je' receln.
SWIOI 12/1'/89 Dote no' JO' ncel..od
SWIOI 01/25/90 Dote no' ro' nce"'od
SWIOI 02/22/90 0.'. not ,at rac.tva.
SWIOI 01/21/90 0.,. not ,at rac.t".d
VAlU[ QUAllflfRS: NA - .n.1~t. not raqu..'ad or an"yta da'. not rat racatvad
... - In.ulflctant S...,. or Aadtoch..'atrr An.',... not ra4wa.'ed.
OIIIA VALlOAJlOM QUAl'UAS: (No nltdotlon quollflo. Indlcoteo dote hu no' boon ..oltdo'od.)
. . .eJec'M,
A . Accoptob'e wl'h quollflco,Iono.
.
..
-------
Total
STATION 59
St..ton
""".r
0.'.
5....'..
Groll A'ph.
pC'/'
taro.. ..t.
pCI/'
""'.
---_._--- --.- ----
..----------
SWOS' 07/21/87 26 ~ 6 28 ~ 6
SW05' 07/01/88 NA NA
SII059 03/20/8' 10 ~ 14 , ~ 7
SIlOS' 05/11/8' JlO ~ 140 340 ~ 100
SIlOS' 06/08/89 Det. not ~.t ...ca'vad
SW05' 07/06/8' 140 ~ 40 It ! 20
SV05' 08/10/8' oet. "ot ,at received
SIlOS. 0'/18/8' 0.7 ~ 2.0 II 0.8 4 ~ ) A .
SIlOS' 10/OJ/8. O.ta not ,at recalvad
SW05. 11/06/8. D... not ,at ra.a'...'
SIlOS. 12/06/89 D... not ,at rac.tved
SWOS' 01/2J/1O D... not ,at rec.Iveet
SVOS' 02/0./10 O.ta not ,at recetvad
SIlOS. OJ/I2/.0 O.ta no' ,.t rac.tved
Surfaae Water
Ra4ioche.istry sampling
Results
1811.
Stra..tt- 8...0
~I/' 1811.
Plutonl- 231
pet/'
AlMrl"'"", 241
~I/I
....
'rttt-
~t/l
....
....
1.0 0.0 ! .,j 0.03.!. 1.4 cliO
NI 0.00 ! 0.219 O.J HI 0.00 1 2tS 1100
-0.1 .!. 0.11 0.48 ! 0.04 0.20 ! o.n no! 1110
0.410.7 O.'~O.I I.J .!. 0.1 70 1 140
-0.1 ~ 0.4 3.1 ! 0.1 0.00 ! 0.01 80! 140
0.1 ~ 0.2 0.3 0.021 ! 0.007 0.006 -0.001 .!. 0.004 0.007 -200 .!. Joo 400
VALUE QUALlfIEAS: Nil . An.I,t. not r.qua.ta. or .n.I,ta ,.t. not ,at r...t....
... - Ift.~'ftct.nt S88p'. or .8dtoc''''ltr, An.',... Rot r.~u..'...
DA'A VALIDAflON QUALfIEAS: (No ...II..tlon qu.'I'I.r In.I..ta. ..t. h.. not ba... ...II..ta..)
I - I.Ja.tad,
A . Ac.apt.bla .Ith qu.II'I..tto...,
v . V.It.
.
-------
Total
8urface Water
Ra4iocbeaistry 8a.pling
8TATION 59
5,.,'on Da" Total Uranl-
H_er Sa...led pCI/1 ..te
swon 01/'l1/81 8.110
SW05. 01/01/88 '.460
swon OJ/'l0/8' 5.500
5\/On 05/11/8' J6 . 600
5\/05' 06/08/" O.'a not Y8,:r8catv8d
5\/On 01/01/8. 0.'l00
5\/05' 98/10/8. Oa.. not ,et recetved
5\/05' 0'1/18/8' 6.800
5\/05' 1°/°1/8. Data not ,at recet"ed
5\/05' II /06/8' Date not ,et rece "'e.
5\/On U/OI/8. Oa.. not ,et receIve.
5\/05' OllUllO 0... not ,et racetvad
5\/05. 0'l,0,/1O Date not ,et racetvad
5\/05' OJI l'lilO Da.. not ,et rae.tvad
YALU[ QUALlfl[AS, NA . Anel,te not requeate. or anal,te .ate not ,et receIved
... . In.yf'tct.nt SI8918 or ..dtoc~..,.try Aft..,... not requ,".d.
DATA VALIDATION QUALfl[AS: ("0 va'Idatlon quallflar In.leatea data haa not baen vaT'.ate..)
It - ReJecte.,
Results
A . Acce.ta~'a .Ith .uallflcatlona.
.
.
-------
',.-
Total
Surfaoe .ater
Radioobe.istry SaapliD9
aesults
STATION 63
St.tton O.t. Gro.. Alpho Grooo 'oto
H_or So...lod ptl/I lOdo ptl/I lOdo
------
swan 01/24/81
SV06J 01/"/88 HA HA
SII06) 0)/28/8' DAY
svon OS/12/U DAY
SV06) 01/21/8' DAY
svon 01/"/" DAY
svon 08/"/8' DAf
svon 0'/15/8' DAY
SVOI) 10/04/U DAf
svon 11/0)/8' DAf
svon 12/01/8' DAf
svon Ol/OS/'O DAY
svon 02/02/'0 DAY
5tro,,"- ".10 Pt"to"l- 2J' "'rlcl- 241 'rlth.
pel/I lOdo pet/I "0 ptl/I lOdo pel/I "'0
----
HA 0.242 : 0.212 0.2 HA 1100 i Jot 100
VAlU( QUAlIFI(AS: HA - A"ol,to not r.quo.tod or o"ol,t. doto not ,ot rocolvod
... . IRIMfftet.nt S.-p'. or Aldtoch"'I'rr ~ft.'r'" nDt r.qu..t.d.
DA'A VALIDATION QUAlFI(AS: ("0 voltdotlon quollftor Indleot.o doto hoo not boo" volldot.d.1
. - .0J.ctodl A - Aceoptoblo .Ith q"ollflcotlo"ol
V - Voltd
.
-------
STATION 63
Station
"...bar
5\IOU
5\IOU
$VOU
5\IOU
5\IOU
5\1011 J
5\IOU
SVOU
5\IOU
5\IOU
5\1011 J
5\IOU
$VOU
Olt.
S....I.d
07/24/87
07/0./88
OJ/28/89
05/12/89
011/21/89
07/19/89
08/11/89
09/15/89
10/04/89
II/OJ/89
12/01/89
01/05/90
02/02/90
Total
Surface Water
Radiochemistry saapling
Tot.' Uranh...
pCI/1
M.
------- .---.--
20.500
DAY
OIlY
DAY
DAY
DAY
DAY
DAY
DAY
DAY
DAY
DAY
VAlU( QUAL If lEAS: HA - An.'". not requ..tad or an.'". data not ~.t ree.tv.d
... . IftlUfllct8ftt 5...18 or A8dfoch...,trr Anal,... not requa.t...
OAf A YALIDAtlON QUALff[AS: (No v.lldatlon qu.llfl.r Indlclt.1 d.ta hll not b... w.II..t...)
. . ..J.ct..;
Results
A . Acc.ptabl. with qu.llflc.tlonll
,
'.
-------
Surface Water
Total Ra4iocheaistry S..pling Results
STATION ,.
St.tton D,U Groa. Alph' GrOll I.ta
H-er So""I,d ,etll lIIdo pC'll Old,
----- ----.-----.-
swou 07/22/87 J4 ! 7 !IJ ! 16
SWOl 4 0"0"88 HA HA
SWOU OJ/JO/8' DAY
SWOU 05/22/8' Data not yet recetyed
swoU 06/27/8' 17 ! 7 ' 17 ! J 4
SWOU 0""'" DAY
SWOU 08/11/8' DAY
swou 09/20/" DAY
SWOU 10/04/8' DAY
swou 11/0"" DAY
swou 12/01/" DAY
SWOU 01/05/'0 DAY
swou 02/02/'0 DAY
Strontt- 8',1NI
pCl/1 "'0
Pluton'u. 2J'
petll
"'0
-----
---.-
1.5
O.I! 1.2
0.12) ! 0.221
0.2
HA
0.1 ~ 0.4
0.00 ~ 0.01
o.
o.
VAlU[ QUAlIFI[AS: NA - Anolrto not roquooted or onolrto dote not rot roco'vod
... - In.ufflct.nt 5...'. or Aa4toch"'ltrr An.'"., not raqy..,.'.
DATA VALIDATION QUAlfl[AS. ("0 volld,tlon quoll"or Ind'c.t.. d.to ho. not b.on v.lld"od.)
_rlcI- 241 Trttl-
pC'll "'0 pCl'l "'0
0.01 ~ J.J cliO
HA 282 ! JOJ 500
0.00 ! 0.01 O. .0 ! 2)0 JI
A - .oJoetedl A - Accop'oblo .'th quol'f'co"onol
V - Volld
,
-------
Total
Surface Water
Ra4iocbeaistry SaapliDg
STATION 64
St.tton 00.0 ToU' Ur."'...
H..ber 50",'od pCl/. lido
-'---
$We4 07/22/.7 11 . ZOO
$\1014 07/01/. 21.11"
$\1014 01/10/.' OIlY
SW014 OS/22/81 DoU no' ,o',rocolvod
SW064 0./21/81 ).600
511064 01/1./.. OIlY
SW064 0./11/.. OIlY
511064 0./20/.t DAY
511064 10/04/81 OAY
SW064 11 /ot/8t DAY
$\1064 12/01/81 DAY
SW064 0'/05/" DAY
511064 02/02/" DAY
VAlU[ QUAllfl[AS: HA . Anol"o no' .oquoo.od 0' 0"0"'0 doto "0' ,ot .ocolvod
... . JRIM"tct.., $88p18 or Aldtoch"'ltr, Aft81,... not r8quel'e4.
DATA VALIDATION QUAlfl[AS: (No volldo'lo" quollflo, I"dlcoto, do'o ho, no' boon v,lld,'od.)
Results
. - .0Joe'ed. A. Accoptoblo with quollflco'lon,.
.
.
-------
Total
Surface Water
Radiocheaistry sa.pling
Results
STATION 103
Stet Ion
H.-ber
0.'.
S..pl.d
Gro.. "I ph.
pCI/1
Gro.. ..ta
pCI/1
5Iro,,"- 8'.90
pCI/1 ....
....
....
------------
--------------
5\/10) 01/11/88 HA HI HI
SWIOI OI/U/88 5J~J8 n ~ 18 -0.1 ~ 0.'
5\/101 OS/25/88 It ~ II 18 ~ 10 -0.1 ~ 0.'
5\/101 06/15/88 ° ~ I I ~ 2 -0.1 ~ 0.11
5\/101 01/U/8' 081. "ot yet recetved
5\/101 08/02/88 Date ..ot ,.t ..u h..
5\/101 0./07/88 14.0 ~ 1.1 2.' 18.1 ~ 1.0 1.4 .11 ~ .18 ..0
5\/10) 10/01/8' 0.\8 not ,.t r.c.h.d
5\/101 11/01/8. Oat. not wet rec.tved
5\/10) 12/H/88 O. \8 flGt ,.t ....h.d
5\/101 01/18/'0 Date not ,.t ....Iv.d
SWIO) 02/12/.0 Oat. lIot ...t recet..d
5\/10) 03/22/90 0.'8 lIot yet rac.t.ad
V"LUE QU"LlfIERS: HA . "".Irt. "ot r.qu..t.d or .n.lrt. d.t. not r" r.c.lv.d
... - 1".u"lcl.nt 5..,1. or ..dlo.h..l.trr "".1,... "ot r.qu..t.d.
DA'" VALIDAIION QU"LfIEA5: (Ho v.lld.tlon qu.II'I.r Indlc.t.. d.t. h.. not b..n v.lldat.d.)
Plutonl- 218 "'rlcl- 241 'rlll-
pCl/I .... pCI/1 "'a pCI/I Ma
-------
0.01128 ~ 0.0'20 0.1 1111 4111 1 110 100
0.14 1 0.01 0.101°.04 "0 ~ 1.0
1.410.1 0.11 1 0.01 100 1 110
0.01 ~ 0.01 0.00 1 0.01 100 ~ 110
.152 ~ .on ° .JIO ~ .090 ° 240 ~ J80 JIO
1 - I.Jact.dl
v - Valt.
" - "cc.ptabl. with quall'lc.tl.....
,
-------
Total
Surface Water
Ra4iocb..istry saapliD9
STATION 103
St.tton o.t. To.ol Ure"t..
H..-ber So.plod pCI/1 .0
_..- - -_.- ..------
SWIO) 07/11/88 7. no
SWIG) 0)/U/8' 7.000
SWIG) OS/25/8' 2.400
SWIO) 01/15/81 0.100
SWIO) 07/ U/8I 0.'. not ,et:r.c.tv8d
SWIG) 08/02/8' 0.'. not ret recetve"
SWIG) 0'/07/8' 2."0
SWIOJ 10/0)/81 Dote no' yo' received
SWIOJ 11/0)/8' O.t. not ,e' rec.tved
SWIOJ 12/08/8' 00 te no' rot rec.tved
SWIO) 01/18/'0 00'0 no' rot rec.tved
SWIOJ 02/12/90 Dolo no' rot rocohod
SWIOJ OJ/22/90 00'0 not yo' rec.t"ed
VALUE QUALlfIEAS: HA - Anetyt. not requ..tad or .n.lyt. data not yet rec.lved
... . Ift.utltctent S...,. or .8dtoch..'atrr An.'"" not r'4u..t.~.
DAIA VALIDATION QUAlflfAS: (No volld.'lon qu.II'lor Indlca'o. do'. ~a. no' boon vallda'od.)
. . .0Jocted.
Results
A . Accop'oblo .I'~ quoll'lco'lon..
t
.
-------
-------
I
APPENDIX C
.'
SURFACE WATER SAMPUNG RESULTS
SUMMARY TABLES
OPERABLE UNIT NO.2
SURFACE WATE" INTERIM REMEDIAl ACTION ~
ROCI('( "I.ATS "':..AIIr.". CiO\.DEN. COLORADO
~&S ~lr&Q ...ntJf 8:)C)8nc.pgl
-------
.'
SuRFACE WATER INTERJIoI RJEIoIEOtAJ.. ACTION PLAN
!'IOCXV F!.,ATS P!.,ANT. GOI.OEN. COIoORADO
~&S .....r8O .,.,n\ot. APe>ena.pgs
I
-.
APPENDIX C
SURFACE WATER SAMPUNG RE.
SUMMARY TABLES
-------
;
w
STATION 53
VOLATILE ORGANIC COMPOUND CONCENTRATIONS
IN SUUACB WATBR
ALL CONCENTRATIONS IN uq/1
Background ARAR NuMb.r 0' NuMb.r 0' R.sults H.. i- Hini- Avaraga of
Anal yh ValtJe". Valu. Ruul ts Abov. ARAR Valua Valu. All Valuas"
Chi orOlll8th.,.,. 10 U 7 0 10.000 U 10 U 5
Br_th..... 10' U 7 0 10.000 U 10 U 5
Vinyl Chlorid. 10 U 2 7 0 10.000 U 10 U. 5 .
Chi oroathen. 10' U 1 0 10.000 U 10 U 5
Methyl an. Chlorid. 5 U SUI 7 2 9 8 . 5 8 4
Acaton. 10 U lOUI 7 I 11 . .5 J ,
C.rbon Di.ul'ld. 5 U SUI 7 0 2 J 2 J 2
I,I-Dichloro.th.na 5 U 7 8 0 5.0000 U 5 U ]
I,I-Dlchloroathena 5 U 5U1 7 0 5.0000 U 5 U .5
1,2-Dlchloro.thana (total) 5 U 5U1 7 .5 42 . 5 U ~.
Chi orofor. 5 U IU 8 0 Diiioo U 5 U. ] .
1,2-Dichloro.th..... 5 U 5 8 0 5.0000 U 5 U .5
Z-Butenon. 10 U 7 0 10.000 U 10 U 5
I,I,I-Trichloro.than. 5 U ZOO 8 0 5.0000 U 5 U .5
Carbon T.trachlorida 5 U 5 8 0 5.0000 U 5 U .5
Vinyl Acetata 10 U 7 0 10.000 U 10 U 5
BronodichlorOMethen. 5 U 7 0 5.0000 U 5 U ]
1,2-0ichloropropen. 5 U 7 0 5.0000 U 5 U .5
cls-I,.5-Dichloroprop.n. 5 U 7 0 5.0000 U 5 U ]
Trichloro.than. 5 U 5 8 I 13. I J 4
DibromochlorOMethana 5 U 7 0 5.0000 U 5 U ]
1,I,2-Trichloroathan. 5 U 5U 8 0 5.0000 U 5 U ]
8.nlanl 5 U 5U 7 0 5.0000 U 5 U ]
Tran.-I,.5-Dlchloroproplnl 5 U 7 0 5.0000 U 5 U ]
Bromo'orlD 5 U 7 0 5.0000 U 5 U .5
4-Methyl-Z-plntenona 10 U 7 0 10.000 U 10 U 5
Z-HIXenonl 10 U 7 0 10.000 U 10 U 5
T.trachlorolthln. 5 U IU 8 0 5.0000 U S U. .5 .
1,I,2,2-Tatrachloro.than. 5 U IU 7 0 5.0000 U 5 U. .5 .
ToIUln8 S U ZOOO 7 0 Z J Z J Z
Ch I orob.nunl 5 U 7 0 5.0000 U 5 U .5
Ethylblnunl 5 U 7 0 5.0000 U 5 U .5
Styrene 5 U 1 0 5.0000 U S U .5
Total Xyl.nu 5 U 7 0 5.0000 U 5 U .5
(+) Valul a.c..d. ARAR; (----) Value ..caad. background; ,- Value .hown i. TBe; .Vhlra no Tolaranca Intlrval, hlgh..t background valul.
..Thl aVlraga I. cu.put.d by 'ir.t d.tar.lning tha arit~tlc ..an conclntration at individual w.lla/.tatlon. and th.n u.lng this data to
computa thl arlt~tic ..an 'or tha wIII./.tatlon. In this group. If a datu. indicat.s non-d.tactad, thl valul uSld In cOMpUtation 0'
tha arit~tic ~.... i. ona-hal' tha Contract Raqulrad Dat.ctlon LI.lt (CRDl)....
NS-No Standard. U-Dltactlon Li.it. J-Pr.eant baiow Detactlon Li.lt. B~ree.nt In 81ank.
Hini_, Melll_, and Av.ragl b...d on all av.ilabla data.
-------
STATION 53
VOLATILE ORGJUfIC COMPOUND CONCENTRATIONS
IN SURPACB WATBR
ALL CONCENTRATIONS IN uq/l
B.ckground ARAR Nu.b.r of Nu.b.r of R.sults ....i- "ini- Av.r.. of
An.lyh V.h..."- V.lu. R..ul u Abov. ARAR V.lu. V.lu. AU V.lu.."
Chior_th8n. 10 U 7 0 10.000 U 10 U 5
Br_th8n. 10' U 1 0 10.000 U 10 U 5
Vinyl Chlorid. 10 U 2 1 0 10.000 U 10 U + 5 +
Cht oro.th8O. 10; U 1 0 10.000 U 10 U 5
"'thyl.n. Chlorid. 5 U 5U1 1 2 9 B + 5 B ,
Ac.ton. 10 U 10Ul 1 L> ~ S J 6
C.rbon Di.ulfld. 5 U 5U1 7 0 Z J 2 J Z
I,I-Oichloro.th.n. 5 U 1 8 0 5.0000 U 5 U ,
1,I~ichloro.th8O. 5 U 5U1 1 0 5.0000 U 5 U ,
1,2-0ichloro.th.n. (tot.l) 5 U 5111 1 S 'Z + 5 U --U+
Chi oroforM 5 U IU 8 0 !)Jjijoo U 5 U + , +
1,2~ichloro.th8n. 5 U 5 8 0 5.0000 U 5 U ,
2-But8Oon. 10 U 1 0 10.000 U 10 U 5
1,I,I-Trichloro.th8ne 5 U 200 8 0 5.0000 U 5 U ,
Cerbon T.tr.chlorld. 5 U 5 8 0 5.0000 U 5 U ,
Vinyl Aut.t. 10 U 7 0 10.000 U 10 U 5
Br~ichlor_th8n. 5 U 1 0 5.0000 U 5 U ,
1,2-0ichloroprop8n. 5 U 1 0 5.0000 U 5 U ,
cis-I,3-Dlchloroprop.n. 5 U 7 0 5.0000 U 5 U ,
Trichloro.then. 5 U 5 8 I 13+ I J ,
Oibromochlor_th8O. 5 U 7 0 roooo U 5 U ,
1,I,2-Trichloro.th8n. 5 U 5U 8 0 5.0000 U 5 U ,
B.nl.n. 5 U 5U 7 0 5.0000 U 5 U ,
Tr8O.-I,"-Dichloroprop.n. 5 U 7 0 5.0000 U 5 U ,
Br_for.. 5 U 7 0 5.0000 U 5 U ,
'-Hethyl-Z-p.nt8non. 10 U 1 0 10.000 U 10 U 5
2-H.x8Oon. 10 U 7 0 10.000 U 10 U 5
T.tr.chloro.th.n. 5 U IU 8 0 5.0000 U 5 U + 3 +
1,I,Z,Z-T.tr.chloro.th8n. 5 U IU 1 0 5.0000 U 5 U + , +
Toluen. 5 U 2000 1 0 Z J 2 J 2
Chtorah.nl.n. 5 U 7 0 5.0000 U 5 U "
Ethylb.nun. 5 U 7 0 5.0000 U 5 U "
Styrene 5 U 1 0 5.0000 U 5 U ,
Tot.1 Xyl.nn 5 U 1 0 5.0000 U 5 U "
(+) V.lu. .xc..d. ARAR; ( ) V.lue .xc..ds b.ckground; . - V.lue .hown i. TBe; -Vh.r. no Tot.r8Oc, Int.rv.I, high.at background vatu..
--Th. .v.r.g. I. co.put.d by flr.t daterMlning the .rlthMetlc "80 conc.ntr.tion .t individu.t w.tta/at.tlon. end then ualng this dat. to
c~t. the .rlth.etic "80 for the wett.l.t.tlon. In thi. group. If. datu. indic.t.. non-detect.d, the v.tu. used in cORlpUt.tion of
the arith.-tic ~en i. on.-hatf tha Contrect R.quir.d D.t.ction LiMit (CRDL)-_..
NS-No Standard. U~at.ctlon Li.it. J-Pr..ent b.tow O.t.ctlon liMit. B-Pre..nt In Bt8nk.
"ini_, "'xi_, and Aver.. b...d on all avait8bt. dat..
V.tt./St.tions in this group: SUDS3
j
-------
. .
"
..
STATION 59
VOLATILB ORG~IC COMPOUND CONCBNTRATIONS
IN SURFACB WATER
ALL CONCBNTRATIONS IN uCJ/l
B.ckground ARAR NuniJer 0' NuMber 0' Results 118,,1- "In i- Averege 0'
An.lyt. V.lue"." V.lue Ruul u Above ARAR V.lu. V.lu. All V.lues""
Chlor...th..... 10 U 1 0 10.000 U 10 U 5
BrOlllOlMth....e Id U 7 0 10.000 U 10 U 5
Vinyl Chlorld. 10 U 2 7 0 10.000 U 10 U + 5 +
Chloroeth..... ui U 7 0 10.000 U 10 U 5
Methylene Chloride 5 U 5U1 7 2 ZO JB + Z J8 ----! +
Acetone 10 U lOUt 7 1 13 8 + 3 J 6
C.rbon Olsulflde 5 U 5U1 7 0 5.0000 U 5.0 U 3
1,1-0lchloroethene 5 U 7 8 Z ill..! 3 J ~+
1.1-0Ichloroeth..... 5 U SUI 7 1 6 J + Z J 3
I,Z-Oichloroethene (tot.l) 5 U 5U1 7 1 H...! 5 U -1D+
Chlorofor. 5 U IU 8 8 82 + 1!...1...! 38 +
1.2-Dlchloroeth..... 5 U 5 8 0 S:-oooo U 5 U -,
2-But....on. 10 U 7 0 10.000 U 10 U 5
1,I,I-Trlchtoroeth....e 5 U 200 8 0 '2 5 U ---1!
Cerbon T.tr.chlorlde 5 U 5 8 8 605 + 160 + --ill +
Vinyl Acet.u 10 U 7 0 iOJiOo U 10 U 5
Bromodichlorometh....e 5 U 7 0 5.0000 U 5.0 U 3
1,2-0ichloroprop....e 5 U 7 0 5.0000 U 5.0 U 3
cis-I,3-0Ichtoropropene 5 U 7 0 5.0000 U 5.0 U 3
Trlchloro.thene 5 U 5 8 8 260 + '9 + 98 +
o ibr080chloraneth....e 5 U 7 0 5.0000 U IT U -,
1,I,2-Trichloroeth....e 5 U 5U 8 0 5.0000 U 5 U 3
Benzen. 5 U 5U 7 0 5.0000 U 5.0 U 3
Tr....s-I,3-0Ichloropropene 5 U 7 0 5.0000 U 5.0 U S
Br08O'or.. 5 U 7 0 5.0000 U 5.0 U 3
'-Methyl-2-pent....one 10 U 7 0 10.000 U 10 U 5
2 -H......one 10 U 7 0 10.000 U 10 U 5
T.tr.chloroethene 5 U IU 8 8 270 + ,,+ -..!! +
1,I,2.2-T.tr.chloroeth..... 5 U IU 7 0 5.0000 U IT U + 3 +
Toluene 5 U 2000 7 0 5.0000 U 5.0 U 3
Chi orubenzene 5 U 1 0 5.0000 U 5.0 U 3
Ethylbennne 5 U 7 0 5.0000 U 5.0 U S
Styrene 5 U 7 0 5.0000 U 5.0 U S
Tot.1 Xylenes 5 U 7 0 5.0000 U 5.0 U S
(+) V.lue ..ceeds ARAR; (-) V.lue uceeds b.ckground; ,- V.tue .hovn I. TBe; -\/here no Toler_e Int.rv.t, hlgfl..t backg"ound v.lu..
"-Th. .verege I. cOMpUted by fl".t d.te,..lnlng the ."Ith.-etlc ...... concentr.tlon .t Ind Iv I duet velt./.t.tlon. end then ullng thl. d8t. to
c~tl thl ."Ith.etlc ...... fo" the vIII./lt.tlon. In thil group. I'. d8tu. Indlc.te. non-detected, thl v.lue u.ed In cOMpUt.tlon o'
the .rlt~tlc me.... is one-hel' the Contr.ct Rlqulred Oet.ctlon li.lt (CRDl)--..
HS-Ho Stenderd. U-Detectlon ll.it. J~r'lent belov Oet.ctlon li.lt. 8~res'"t in Blenk.
"inl_, 118111_, end Averege ba..d on .11 .v.llebl. det..
-------
STATION 59
VOLATILE ORGANIC COMPOUND CONCENTRATIONS
IN SURI'ACB WATBR
ALL CONCENTRATIONS IN uq/l
B.ckground ARAR ~.r of NuMb.r of R.sults H8x 1- "Inl- Av.rag. of
An.lyh V.lu.... Velu. Ruuhs Above ARAR Velu. Valu. Att V.lu.s"
ChtorOlMthan. 10 U 7 0 10.000 U 10 U S
Br--thane Id U 1 0 10.000 U 10 U 5
Vinyl CMorid. 10 U Z 1 0 10.000 U 10 U + 5 +
ChI oro. than. 10 U 7 0 10.000 U 10 U 5
Methyl.n. Chlorld. 5 U 5U1 1 Z 20 JB + Z JB -!+
Auton. 10 U 1 QUI 1 1 13 B + 3 J 6
C.rbon Olsulfld. S U SUI 7 0 5.0000 U 5.0 U 3
1,I-Olchloro.th.n. S U 7 8 Z ill....! 3 J -1.1 +
I, I-DI chI oro. thane S U 5UI 1 1 6 J + Z J 3
I,Z-Dlchloro.th.n. (total) 5 U SUI 7 1 ~ 5 U --1! +
CMorofor. 5 U IU 8 8 82 . .1!.J...! ---11+
.I,Z-olcMoro.than. 5 U 5 8 0 s.-oooo U 5 U 3
2-Butanon. 10 U 7 0 10.000 U 10 U 5
1, I, I-Trlchloroethan. 5 U 200 8 0 g 5 U --1!
C.rbon T.trachlorld. 5 U 5 8 8 605 . 160 + -ill +
Vinyl Ac.taU 10 U 7 0 1O:oiio U 10 U 5
Bromodl chI oromsthan. 5 U 7 0 5.0000 U 5.0 U 3
1,2-Dichloropropane 5 U 1 0 5.0000 U 5.0 U 3
cis-I,3-0ichloroprop.n. 5 U 1 0 5.0000 U 5.0 U 3
TrlcMoro.then. 5 U 5 8 8 260 + ". ---H +
Dibromochlora.8than. 5 U 1 0 5.0000 U IT U 3
1,I,2-Trlchloro.than. S U 5U 8 0 5.0000 U 5 U 3
B.nun. S U 5U 7 0 5.0000 U 5.0 U 3
Trans-I,3-Dlchloroprop.n. 5 U 7 0 5.0000 U 5.0 U 3
Bromoforlll 5 U 1 0 5.0000 U 5.0 U 3
'-Methyl-2-p.ntanon. 10 U 1 0 10.000 U 10 U 5
2-Hu_. 10 U 7 0 10.000 U 10 U 5
T.trachloroethena 5 U IU 8 8 ~70. ". 9' .
1,I,2,Z-T.trachloroethan. 5 U IU 1 0 5.0000 U IT U. ~+
Tolu.n. 5 U 2000 1 0 5.0000 U 5.0 U 3
CM orob.nun. 5 U 7 0 5.0000 U 5.0 U 3
Ethylb.nun. 5 U 7 0 5.0000 U 5.0 U 3
Styr.ne 5 U 7 0 5.0000 U 5.0 U 3
Total Xyhnn 5 U 7 0 5.0000 U 5.0 U 3
(+) Valu. .xc..ds MAR; (-) Value exce.ds background; . - Valu. sho,," Is TBe; -\/h.rs no ToIsr-e Inurval, hlgh.st background valu..
..The average Is c08pUted by first dat.~lnlng the arlt~tlc ..en conc.ntration at Individual v.tt./statlons end th.n using this deta to
c08pUt. th. arith8etlc ..en for the v.II./.tetlons In lhi. group. If a delU. Indicates non-d.lected, lh. value used In cOMpUlatlon of
the arlthn.tlc ..en Is one-half the Contract R.qulr.d D.t.ctlon ll.ll (CRDl)..-.
HS-No Standard. U-o.t.ctlon lI.lt. J-Prs..nt b.lov Deuctlon lI.ll. B-Pruent In Blenk.
"Inl_, H8xl_, end Av.rag. bal.d on all availabl. deta. .
V.IIs/Slallons In this group: SV059
~
-------
..
....
STATION 64
VOLATILE ORGANIC COMPOUND CONCENTRATIONS
1M SURPACB WATER
ALL CONCBNTRATIOMS IN uq/l
B.ckground ARAR "'-'ber 0' NuMber 0' Results "'.1- Hlnl- AY8rege 0'
AnIIlyte Velue." V.lue Re.ul u Above ARAR V.lue Velue AU Velue."
Chlor--th- TT 3 0 10.000 U 10 U 5
Br_thene 3 0 10.000 U 10 U 5
Vinyl Chloride 10 U 2 3 0 10.000 U 10 U + 5 +
Chloroethene 10 U 1 0 10.000 U 10 U 5
Methylene Chloride 5 U SUI 1 1 9 B + 5 U 5
Acetone 10 U lOUt 1 0 5 J 2 J ,
C.rbon DI.ul'lde 5 U SUI 3 1 i..! 5 U ,
1.1~lchioroethene S U 7 , 0 5.0000 U S U 1
1.1~lchloroethene S U SUI 3 0 5.0000 U S U 1
1.2~lchloroethene (totel) 5 U SUI 3 0 5.0000 U 5 U 3
Chloro'or. 5 U IU , 1 lL.! 1 J -1+
1.2~lchloroethene S U 5 , 0 5.0000 U S U 1
2-Butenone 10 U 1 0 10.000 U 10 U 5
1.I.I-Trlchloroethene 5 U 200 , 0 5.0000 U 5 U 3
C.rbon Tetrechlorld. 5 U 5 , 0 1 J 1 J 1
Vinyl Acetete 10 U 1 0 10.000 U 10 U 5
Bronodlchlor--thene 5 U 3 0 5.0000 U 5 U 1
1.2-Dlchloropropene 5 U 3 0 5.0000 U 5 U 1
cls-I.1~lchioropropene 5 U 1 0 5.0000 U 5 U 1
Tr Ichloroethene 5 U 5 , 1 l.!!..! 5 U -1}+
Olbru.ochlor--thene 5 U 1 0 5.0000 U 5 U 1
I.I.2-Trlchloroethene 5 U 5U , ° 5.0000 U 5 U 1
Bennne 5 U 5U 1 ° 5.0000 U 5 U 1
Trens-I.1~lchioropropene 5 U 1 0 5.0000 U 5 U 1
BrOlllO'or. 5 U 3 ° 5.0000 U 5 U 1
'-H8thyl-2-pentenone 10 U 1 ° 10.000 U 10 U 5
2-He.enone 10 U 1 ° 10.000 U 10 U 5
Tetrechloroethene 5 U IU , ° 5.0000 U 5 U + 1 +
I.I.2.2-Tetr.chloroethene 5 U IU 1 ° 5.0000 U 5 U + 1 +
Toluene 5 U 2000 1 0 5.0000 U 5 U 1
Chi orobenKene 5 U 1 0 5.0000 U 5 U 1
Ethylbennne 5 U 1 ° 5.0000 U 5 U 1
Styrene 5 U 1 ° 5.0000 U 5 U 3
Totel Xylen.. 5 U 1 ° 5.0000 U 5 U 1
(+) V.lue e.ceeds ARAR; ( ) V.tue "Cleds background; ,- V.lue shown is TBe; .Uhere no Toler_e Intervel. highest beckground velue.
.8The everege Is c~ted ~Irst deter.lnlng the .rlth8etlc ..en concentr.tlon .t Individual wells/st.tlons end then using this dat. to
c~t. the .rlth8etlc ..en 'or the wells/st.tlons In this group. I'. datu. Indlcetes non-detected. the v.lue used In cOMpUt.tlon 0'
the erlth8etlc ..en Is one-he I' the Contr.ct Required Oetectlon ll.lt (CRDL)---.
HS-No Stenderd. U~euctlon lI.it. J-Pre..nt below Oetectlon lI.lt. B-Pr..ent In BI....
Hlnl_. "'.1_. end Aver...e bend on .U ev.ilabl. dat..
-------
STATION 64
VOLATILB ORGANIC COMPOUND CONCENTRATIONS
IN SURPACB WATBR
ALL CONCBNTRATIONS IN uq/l
BeckgrCM.nd ARAR ttu.ber of ttu.ber of Results "-lCi- "in i- Aver.... of
Anelyte Velue"'. V.lue R..ul u Above ARAR V.lue V.lue AU Velue.'"
CMor--th_ ;n- S 0 10.000 U 10 U 5
Br_thene J 0 10.000 U 10 U ~
Vinyl CMor Ide 10 U Z J 0 10.000 U 10 U + 5 +
CMoroethene 10 U J 0 10.000 U 10 U 5
"-thytene Chloride 5 U 5U1 J 1 ' 8 + ~ U 5
Acetone 10 U 10U1 J 0 5 J Z J 4
Cerbon Ol.ulflde 5 U 5U1 J I ~ 5 U 4
1.I~ichloroethene 5 U 7 4 0 5.0000 U ~ U J
I.I~ichioroethene 5 U SUI J 0 5.0000 U 5 U J
I.Z~lchioroeth8ne (tote I) 5 U SUI J 0 5.0000 U 5 U J
CMorofor. 5 U IU 4 I fi..! 1 J --1+
I.Z~lchioroethane 5 U 5 4 0 5.0000 U 5 U J
Z-Butenone 10 U J 0 10.000 U 10 U 5
I. I. I-Trichloroethene 5 U ZOO 4 0 5.0000 U 5 U J
Cerbon Tetr.chloride . 5 U 5 4 0 J J J J J
Vinyl Ac.tete 10 U J 0 10.000 U 10 U 5
BrOftOdI chi oro..thene 5 U J 0 5.0000 U 5 U J
I.2-Dichtoropropene 5 U S 0 5.0000 U 5 U J
cls-I.J~lchloropropene 5 U J 0 5.0000 U 5 U J
T r I cM oroethene 5 U 5 4 J l!..! 5 U ----1} +
DibrOMOchioro..then. 5 U J 0 5.0000 U 5 U S
I.I.Z-Trichloroethene 5 U 5U 4 0 5.0000 U 5 U J
Ben.ene 5 U 5U J 0 5.0000 U ~ U J
Trens-I.S-Dichtoropropene 5 U J 0 5.0000 U 5 U J
BrOlllOfor. 5 U J 0 5.0000 U ~ U J
44H1thyl-Z-pentenone 10 U J 0 10.000 U 10 U 5
Z-H8ICenone 10 U J 0 10.000 U 10 U 5
Tetrechloroethene 5 U IU 4 0 5.0000 U 5 U + S +
I.I.Z.Z-Tetrechloroethane 5 U IU J 0 5.0000 U 5 U + S +
Totuene 5 U ZOOO J 0 5.0000 U 5 U J
CM orobenzene 5 U J 0 5.0000 U 5 U J
Ethylbenzene 5 U J 0 5.0000 U 5 U J
Styrene 5 U S 0 5.0000 U 5 U S
Total Xylen.. 5 U 3 0 5.0000 U 5 U 3
(+) V.lue elCceeds ARAR; . ( ) Value elCceed. beckgrCM.nd; ,- Velue .hovn i. TBC; .Vhere no Tolerenee Interv.I. hlghe.t beckgrCM.nd v.lue.
..The avereg. I. c~ted ~ir.t deter.lnlng the .rithe8tlc ..en concentr.tlon et Indivlduat velte/.tetlon. end then u.lng thl. data to
c~te the erlth8etic ..en for the vell./.tatlon. In thl. group. If e datu. Indicate. non-detected. the velue u.ed In c~tation 0'
the arlth8etlc ..80 Is one-hatf the Contract Required Detection ll.lt (CROt)....
NS-No Standard. U-oetectlon ll.it. J-Pre.ent belov Detection ll.lt. B-Pre.ent In Blenk.
"In 1_. HelCi_. end Aver...e ba..d on aU .v.Heble data.
Vell./Stetions In this group: SV064
.
-------
....
..
...
903-PAD AND LIP SITB
DISSOLVBD MBTAL CONSTITUBNT CONCENTRATIONS
IN SURFACB WATBR
ALL CONCENTRATIONS IN 8q/l
D.tection B.ckground ARAR . tUIob.,. 0' NuMb.,. 0' R.sults "'"1- Hini- Ave,..... 0'"
An.lyt. limit." V.~u.. V.lue Rnul u Abov. ARAR V.lue V.lue All V.lun
Ah..lnu8 (At) 0.0290 0.~850 . 5.0 24 0 .899 .0300 U O. "17
Ant l.ony (Sb) 0.0600 0,'(1600 U 0.06U 18 ° 0.0600 U .040 U 0.0300
A,...nic (As) 0.0100 0.0100 U 0.2SU 18 0 0.0100 U .0020 U O.OOSO
B.d..... (B.) 0.0100 0.2000 U 1.0 U 0 !U .200 U 0.2035
Berytl lun (B.) O.OOSO 0.0050 U O.OOS 18 0 0.0050 U .0020 U 0.0025
C8dnil8 (Cd) O.OOSO 0.0050 U 0.01 18 ° O.ooSO U .0040 U 0.0025
C.lei..... (C.) 0.7500 85.9230 HS 2~ 0 156 72.30 ---1!!
Cesiun (Cs) 0.0200 1. 0000 U 1.0 13 0 iJ.ii2oo U .0010 U 0.0100
Ch,._lun (Cr) 0.0100 0.0100 U 0.05 24 0 0.0100 U 0.01 U 0.0050
Cob.1 t (Co) 0.0220 0.0500 U 0.05 24 0 0.0220 U .0200 U 0.0110
Copp." (Cu) 0.0063 0.0250 U 0.2 24 0 .0279 .0200 U 0.0057
I,.on (Fe) 0.0069 1. 7800 . 0.3 24 4 1.48 + .0554 0.1581
L..d (Pb) O.OOSO 0.005S . O.OS 18 0 .0126 .0020 U 0.0031
Lith I... (LI) 0.1000 0.1000 U 2.S 13 ° .179 .0795 0.0662
Hagnn 118 (Hg) O.OSOO 12.8150 HS 2~ 0 28.30 7.54 --1i
Hengenue (....) 0.0051 . 0.3680 . 0.05 24 17 1.64 + 0.015 U 0.2427 .
",,.cury (Hg) 0.0002 0.0003 . 0.002 18 0 JiiiiiJ .0002 U 0.0001
Hot ybd.num(Ho) 0.0220 0.1000 U O. I 19 0 .0201 .0201 0.0112
Hicht (Hi) 0.0370 0.0400 U 0.20 24 0 0.0370 U .0200 U 0.0185
Potus iUII (K) 0.5000 5.0000 U HS 18 0 9.04 2.42 1.0591
S.teniun (58) 0.0050 0.0050 U 0.01 18 I .0134 + .0020 U 0.0031
Sit vsr (Ag) 0.0076 0.0100 U O.OS 24 0 0.0076 U 0.01 U 0.0038
Sodium (N.) 2. 1000 46.2450 NS 24 0 88.50 7.04 28
St,.ont iUII (Sr) 0.0200 0.3960 NS 24 0 ~ .389 0."80
1h.ltiUIII (11) 0.0100 0.0100 U O.OIU 18 0 0.0100 U .0030 U 0.0050
Tin (Sn) 0.1000 0.1000 U O. I 13 0 0.1000 U .100 U 0.0500
V_dIUII (V) 0.0240 0.0500 U 0.1 24 0 0.02~0 U .0100 U 0.0120
llnc (In) 0.0200 0.0320 . 2.0 24 0 .Ll! 0.02 U .Jl.l.ill
(.) V.tu. un.ds ARAR;. (-) V.tue un.ds b.ekground; ,- V.tu. shown it TBC; .tlher. no Toter_. Interv.t, hlgh..t beckground v.tue.
..Th. .V."89S is eomput.d by 'I,.st deter.lnlng the .rithMetle ..en concentr.tion .t indivlduel w.tts/st.tlons end thsn using this det. to
computs the .rlth.8tlc ..en '0,. the wstt./st.tion. In thl. group. I'. detUM Indlc.ts. non-dst.ctsd, ths v.tus u.ed in cOMpUt.tlon 0'
the .,.lthMetic ..en is one-h.t' the Cont,..ct Requl,.ed D.tectlon LI.lt (CRDL)....
NS-Ho Stend.,.d. U-Detectlon Li.it. J-p,.e.ent betow Oetectlon li.lt. B-p,.e.ent In Btenk.
HiniMU8, ....i_, end Ave"8ge b..ed on .It .v.lteble det..
-------
.. . ~
""'
I03-PAD AND LIP SITB
DISSOLVBD MBTAL CONSTITUBNT CONCBNTRATIONS
IN SURWACB WATBR
ALL CONCBNTRATIONS IN 89/1
Detect ion Beckground ARAR "'-ber of NuMber of Resutts "'Jti- Hini- Aver.. ofu
Anetyte Lilllitu. Vetue. Vetue R..ut ts Above ARAR Vetue Vetue Alt Vetun
Ah.. ima (At) 0.0290 : O.48SO .. 5.0 2' 0 .899 .0300 U O. "17
Ant l.ony (Sb) 0.0600 0.'0600 U 0.06U 18 0 iiJiioo U .040 U 0.0300
Arsenic (As) 0.0100 " 0.0100 U 0.25U 18 0 0.0100 U .0020 U 0.0050
eerlUli (Be) 0.0100 0.2000 U 1.0 24 0 1M .200 U 0.2035
eerytllUli (Be) 0.0050 0.0050 U 0.005 18 0 0.0050 U .0020 U "1[ijffi
Cech I UIII (Cd) 0 .OOSO 0.0050 U 0.01 18 0 0.0050 U .0040 U 0.0025
Cet c h... (Ce) 0.7500 85.9230 NS 24 0 156 72.30 ~
CnlUIII (C.) 0.0200 1.0000 U 1.0 13 0 0.0200 U .0010 U 0.0100
ChrOlll h... (Cr) 0.0100 0.0100 U 0.05 24 0 0.0100 U 0.01 U 0.0050
Cobet t (Co) 0.0220 0.0500 U 0.05 24 0 0.0220 U .0200 U 0.0110
Copper (Cu) 0.0065 0.0250 U 0.2 24 0 .0279 .0200 U 0 . 0051
Iron (Fe) 0 .00&9 1. 7800 .. 0.3 24 , 1.48 + .055' O. 1581
L..d (Pb) 0.0050 0.0055 .. 0.05 18 0 .0126 .0020 U 0.0031
LithlUl'/l (LI) 0.1000 0.1000 U 2.5 13 0 .179 .0795 0 . 0662
"'911" I UIII (Hg) 0.0500 12.8150 NS 2' 0 28.30 7.5' ---1t
Hangene.. (~) 0.0051 0.3680 .. 0.05 2' 17 1.64 + 0.015 U 0.2'27 +
Mercury (Hg) 0.0002 0.0003 .. 0.002 18 0 .0003 .0002 U 0.0001
Hot ybdenun(Ho) 0.0220 0.1000 U 0.1 19 0 .0201 .0201 0.0112
Hicket (Hi) 0.0370 0.0'00 U 0.20 24 0 0.0310 U .0200 U 0.0185
Pota., lUll (K) 0.5000 5.0000 U HS 18 0 9.0' 2.42 I. 0591
SehniUl'/l (Se) 0.0050 0.0050 U 0.01 18 I .0134 + .0020 U 0.0031
Sit ver (Ag) 0.0076 0.0100 U 0.05 2' 0 0.0076 U 0.01 U 0.0038
SodlUII (He) 2. 1000 46.2'50 HS 2' 0 88.50 7.04 28
Stront IUI'/I (Sr) 0.0200 0.3960 HS 2' 0 ~ .389 0.4180
Ihelt iun (n) 0.0100 0.0100 U O.OIU 18 0 0.0100 U .0030 U ""iJi05ii
IIn (511) 0.1000 0.1000 U 0.1 U 0 0.1000 U .100 U 0.0500
V_dIUII (V) 0.02'0 0.0500 U 0.1 24 0 0.02'0 U .0100 U 0.0120
Zinc (In) 0.0200 0.0320 . 2.0 2' 0 1.26 0.02 U Jl.:.ill!
(+) Vatua e.ceed. ARAR; ( ) Vatue e.ceed. beckground; , - Vatue .hown is TBe; .Uhere no Toterenea Intervet, hlghe.t beckground yetue.
..lhe average i. c~ted by fir.t detar.inlng the arlth.etlc ..an concentretlon et indiylduat vette/.tetlon. end then u.lng tht. dat. to
c~te the arlth.etlc ..an for the vett./etetlon. In thl. group. If a datu. Indlc.te. non-detected, the v.tue u.ed in cOMpUt.tion of
the erlth-etlc ....80 is one-hetf the Contrect R.qulred Detection LI.lt (CROL)..".
HS-No Stendard. U-Oetectlon li.it. J-Pre.ent betov Detection Li.it. B-Pre.ent In Btenk.
Hinl_, ....i_, end Average be.ed on ett eveltebte date.
Vett./Station. in this group: SV050, SVOSI, SVOS2, SVOSS, SVOS7, SVOS8, SV077
-"
-------
.
...
'..,
SOUTH WALNUT CREEK
DISSOLVED METAL CONSTITUENT CONCENTRATIONS
IN SURFACB WATBR
ALL CONCENTRATIONS IN 8CJ/l
.
Detect Ion Beckground ARAR ~er 0' NuMber 0' Results ...,,1- "In 1- Aver.. 0''''
Analyte lilllitAU ValueA Value Ruults Abova ARAR Value Value All Valuee
AIUllinulll (AI) 0.0290 O.USO A S.O 27 0 0.0290 U .0300 U 0.01'S
Ant IIIIonY (Sb) 0.0600 0.d6oo U 0.06U 2' 0 0.0600 U 0.060 U 0.0300
Arsenic (As) 0.0100 0.0100 U 0.2~U 2' 0 0.0100 U .0020 U O.OOSO
Bari- (Ba) 0.0100 0.2000 U 1.0 27 0 ..ill .163 0.0~80
BerylllUil (Ba) O.O~O 0.0050 U 0.005 2' 1 .0053 + .0020 U 0.0026
CachiUli (Cd) O.OOSO 0.0050 U 0.01 2' 0 o.oo~o U .00'0 U 0.0025
Calc h.. (Ca) 0.7500 85.9230 NS 27 0 ill 7.72 74
C..I- (Ce) 0.0200 1. 0000 U 1.0 20 0 0.0200 U .0010 U 0.0100
ChrOlllI... (Cr) 0.0100 0.0100 U 0.05 27 0 0.0100 U 0.01 U 0.0050
Cabal t (Co) 0.0220 0.0500 U 0.05 27 0 0.0220 U .0200 U 0.0110
Copper (Cu) 0.0063 0.0250 U 0.2 Z7 0 0.0063 U .0200 U 0.0032
Iron (Fa) 0.0069 1. 7800 .. 0.3 27 0 0.2 .0302 0.037'
lead (Pb) O.ooSO 0.0055 .. 0.05 2' 0 .~, .0020 U 0.0026
lith 1- (lI) 0.1000 0.1000 U 2.5 20 0 .0200 .0100 U 0.0"2
"'gn..l... (Hg) o. o~oo 12.8150 NS 27 0 U 5.0 U 12
Henganua (Hn) O.OOSI 0.3680 .. 0.05 27 8 .641 + .0100 U 0.10" +
Hercury (Hg) 0.0002 0.0003 .. 0.002 2' 0 0.0007 .0002 U 0.0002
Hol ybdenUII(Ho) 0.0220 0.1000 U 0.1 Z3 0 .02'5 .0100 U 0.0116
Nickel (NI) 0.0370 0.0'00 U 0.20 27 0 0.0370 U .0200 U 0.Ol8S
Potan lUll! (I() O.Sooo S.oooo U NS 2' 0 1.12 .Sl9 0.290S
SelenlUIII (Se) O.OOSO O.OOSO U 0.01 2' 0 .0050 .0020 U 0.0026
Sliver (Ag) 0.0076 0.0100 U 0.05 27 0 0.0076 U 0.01 U 0.0038
Sodl- (He) 2. 1000 '6.2'50 NS 27 0 tM !i U 30
Stront i- (Sr) 0.0200 0 . 3960 NS 27 0 U 0.02 U 0.1936
ThalllUil (Tl) 0.0100 0.0100 U O.OIU 2' 0 0.0100 U .0030 U O.OOSO
Tin (Sn) 0.1000 0.1000 U 0.1 20 1 ~ .100 U 0.0797
Vanad lUll (V) 0.02'0 0.0500 U 0.1 27 0 0.02'0 U .0100 U 0.0120
Zinc (In) 0.0200 0.0320 .. 2.0 27 0 ~ 0.010 ..9...!.l!!
(+) Value a"ceeds ARAR; ( ) Value e"ceed. b.ckground; , - Value .hown I. TB(; AVhere no Tolerance Interval, hlghe.t background value.
A.The average Ie cu.puted by flret deter.lnlng the arithMetic ..an concentration at Individual vella/etatlon. and then u.ing this data to
computa tha arith88tic ..an 'or tha vell.l.tatlon. In thl. group. If a datu!! indicatas non-detected, tha value used In cu.putatlon of
the arlth8etic ..an is one-half the Contract Required Detection ll.lt (CRDl)..".
NS-No Stand.rd. U-Detectlon liMit. J-Pre.ent belov Datectlon liMit. B-Present in Blank.
"ini_, "'"i_. and Avarage ba.ed on all avallabla data.
-------
SOUTH WALNUT CREEK
DISSOLVED METAL CONSTITUENT CONCENTRATIONS
III SURI'ACB WATBR
ALL COIICBNTRATIONS IN 89/1
Oetect Ion Beckground ARAR """er 0' Number 0' Results He. i..... "In 1- Aver.... 0'"
Anal yte li",ltu. Value- Value Ruul u Above ARAR Value Value AU Values
AIUllinull (AI) 0.0290 0.'850 . 5.0 27 0 0.0290 U .0300 U 0.01'5
Ant "lion)' (Sb) 0.0600 0.0600 U 0.06U 24 0 0.0600 U 0.060 U 0.0300
Arsenic (As) 0.0100 0.0100 U 0.25U 2' 0 0.0100 U .0020 U O.ODSO
BedUII (Ba) 0.0100 O.zOOo U 1.0 Z7 0 ..ill .163 0.OS80
BeryH It... (Be) O.OOSO O.OOSO U 0.005 2' I .0053 + .0020 U 0.0026
Cac:hiUIII (Cd) O.OOSO 0.0050 U 0.01 24 0 0.0050 U .0040 U 0.0025
Cel clun (Ca) 0.7500 85.9230 NS 27 0 131 7.72 U
Cnlun (Cs) 0.0200 1. 0000 U 1.0 20 0 0:0200 U .0010 U 0.0100
ChrOlllIUIII (Cr) 0.0100 0.0100 U O.OS 27 0 0.0100 U 0.01 U 0 .00SO
Cabal t (Co) 0.0220 O.OSoo U 0.05 Z7 0 0.0220 U .0200 U 0.0110
Copper (Cu) 0.0063 0.0250 U 0.2 27 0 0.0063 U .0200 U 0.0032
Iron (Fe) 0.0069 1. 7800 . 0.3 21 0 0.2 .0302 0.03U
leed (Ph) 0.0050 0.0055 . 0.05 2' 0 .OOS' .0020 U 0.0026
lithlUII (lI) O. 1000 0.1000 U 2.5 20 0 .0200 .0100 U 0.0462
ttegnnlUIII (Hg) o. OSOO 12.8150 NS 27 '0 l1 5.0 U 12
Hengenua (K-t) 0.0051 0.3680 . O.OS 27 8 .6U + .0100 U 0.10" +
Hercury (Hg) 0.0002 0.0003 . 0.002 24 0 0.0007 .0002 U 0.0002
HoI)'bdel1Ull(Ho) 0.0220 0.1000 U 0.1 23 0 .0245 .0100 U 0.0116
Nickel (NI) 0.0370 0.1'00 U 0.20 27 0 0.0370 U .0200 U 0.0185
PotauiUII (K) 0.5000 5.0000 U "S U 0 1.12 .589 0.2905
SehnlUII (Sa) O.ODSO 0.0050 U 0.01 24 0 .0050 .0020 U 0.0026
SH ver (Ag) 0.0076 0.0100 U 0.05 27 0 0.0076 U 0.01 U 0.0038
Sodl.... (He) 2. 1000 '6.2'50 NS 27 0 !M 5 U 30
Stront iUII (Sr) 0.0200 0.3960 "S 27 0 !!:J 0.02 U 0.1936
ThelllUIII (Tt) 0.0100 0.0100 U O.OIU 2' 0 0.0100 U .0030 U O.ODSO
Tin (Sn) 0.1000 0.1000 U 0.1 20 I U .100 U 0.0797
Vaned lUll (V) 0.02'0 O.OSOO U o. I 27 0 0.02'0 U .0100 U 0.0120
Zinc (In) 0.0200 0.0320 . 2.0 27 0 !U! 0.010 ...!.:..!M!
(+) Value e.ceeds ARAR; (----) Value e.ceeds background; . - Value shoun I. TBC; -Vhere no Tolerance Interval, hlgheet background value.
--The ever age Is co.puted by 'Ir.t deter.lnlng the arithmetic ..en concentration et Individual well./.tatlons and then u.ing thle data to
compute the arith8etic 1118en 'or the walls/stations In this group. I' a datUII Indicatas non-detected, the value used In co.putatlon 0'
the arithMetic 1118en Is on.-half the Contract R.quired Detection ll.lt (CRDL)._..
NS-No Stendard. U-Oetection li",it. J-Pre.ent below Oetectlon ll",lt. B-Present in Blank.
"ini_, He.i_, and Average b.s.d on all avallebla data.
U.lls/Stations in thl. group: SU056 , SU060, SU061, SUIOI
..
-------
~
..
STAT:lON 63
DISSOLVED METAL CONSTITUENT CONCENTRATIONS
:III SURI'ACE WATER
ALL CONCENTRATIONS IN 8g/1
DeUct Ion Beckground ARAR Number 0' Number 01 Resutts Hex I...un. Hinlllll.lll A"erege 0'..
Anet yU limit"'. Vetue. Vetue Rnutts Abo"e ARAR Vetue Vetu. Att Vetues
Atunlnurn (At) 0.0290 0.'8~0 '" ~.O 2 0 0.033 0.033 0.0238
Ant lmony (Sb) 0.0600 0.0500 U 0.06U I 0 0.0600 U O.~OO U + 0.0300
Arsenic (As) 0.0100 0.0100 U 0.2~U 1 0 0.003 0.003 0.0030
Berlun (Be) 0.0100 0.2000 U 1.0 2 0 0.10' 0.10' O.O~,~
Berytt lun (Be) 0.00~0 O.OO~O U O.OO~ 1 0 0.00~0 U 0.002 U 0.002~
Cedmlun (Cd) O.OO~O O.OO~O U 0.01 1 0 0.00~0 U 0.00' U 0.002~
Cet c lun (Ce) ° . 1~00 8~.9230 NS 2 ° ill !.lJ! 103
Ceslun (Cs) 0.0200 1. 0000 U 1.0 0 0 ~
Chromlun (Cr) 0.0100 0.0100 U O.O~ 2 0 0.0100 U 0.01 U o.oo~o
Cobet t (Co) 0.0220 0.0500 U O.O~ 2 0 0.0220 U 0.020 U 0.0110
Copp.r (Cu) 0.0063 0.02~0 U 0.2 2 0 0.0063 U 0.020 U 0.0032
Iron (Fe) 0.0069 1. 1800 '" 0.3 2 0 0.062 0.062 0.0321
L.ed (Pb) O.OO~O O.OO~~ '" O.O~ 1 0 O.OO~ O.OO~ O.OO~O
li th lun (li) 0.1000 0.1000 U 2.~ ° 0 .......
~nlUIII (He) O.O~OO 12.81~0 NS 2 0 HJ1 &l ---ll
Heng80ue (K,) 0.00~1 0.3680 '" O.O~ 2 2 0."2 + ~ 0.'02~ +
Mercury (He) 0.0002 0.0003 . 0.002 1 0 ir.iiiiii2 U 0.0002 U If.1iOOi
H01ybdenurn(Ho) 0.0220 0.1000 U 0.1 1 0 0.0220 U 0.0' U 0.0110
Hlcket (HI) 0.0310 0.0'00 U 0.20 2 0 0.0310 U 0.020 U 0.Ol8~
Pot... lun (I() o. ~OOO ~.OOOO U NS 1 0 1.~' 1.~' 1 . ~'OO
Selenium (Se) O.OO~O O.OO~O U 0.01 1 0 O.OO~O U O.OO~ U 0.002~
Sit "er (Ag) 0.0016 0.0100 U O.O~ 2 0 0.0016 U 0.01 U 0.0038
Sodl"", (He) 2.1000 ".2'~0 NS 2 0 110 102 106
Stroot lum (Sr) 0.0200 0.3960 NS 2 0 1.25 Di1 ...-:16iiO
Thettlun (n) 0.0100 0.0100 U 0.010 1 0 0.0100 U 0.300 U + O.OO~O
Tin (50) 0.1000 0.1000 U 0.1 0 0 .......
V80edlun (V) 0.02'0 o.o~oo U 0.1 2 0 0.02'0 U 0.010 U 0.0120
Zinc (In) 0.0200 0.0320 . 2.0 2 0 0.03 0.028 0.0290
(+) Vetue exceeds ARAR; (----) Vetue exceeds beck ground; ,- V.tue shovn is 'Be; '"Uh.re no Toterence Inter".t, highest b.ckground "etue.
..The ."er.ge Is comput.d by 'Irst deter.inlng the .rithmetic M880 concentr.tlon .t Indi"lduat vetts/st.tlons end then using this date to
compute the .rlthMetic mean 'or the vetts/st.tlons in this group. I'. datun Indlc.tes non-detected, the ".tue us.d In computet Ion 0'
the erlthmetlc me80 Is one-het' the Contr.ct Required Oetectlon Li.lt (CROL)..".
HS-Ho Stenderd. U-Oetectlon Li.it. J-Present b.tov Detection LI.lt. B-Pres.nt in Btenk.
Hini~, Hexl~, end A"erege besed on .tt .".Itable det..
-------
.. .
STATION 63
DISSOLVED METAL CONSTITUENT CONCENTRATIONS
IN SURI'ACE WATER
ALL CONCENTRATIONS IN 89/1
Deuct ion Background ARAR NudJer of NudJer 0' Results Hex i- Hini- Avarege of'"
Anal yU limit." Value. Value Rnul is Above ARAR Value Value All Val un
AIUllinum (AI) 0.0290 0.'8S0 . ~.o 2 0 0.033 0.033 0.0238
Ant imony (Sb) 0.0600 0.0500 U 0.06U I 0 0.0600 U O.~OO U + 0.0300
Arsenic (As) 0.0100 0.0100 U 0.2,)U I 0 0.003 0.003 0.0030
BariUII (Ba) 0.0100 0.2000 U 1.0 2 ° 0.10' 0.10' 0.0~'5
Beryllil.lll (Be) 0.0050 0.0050 U 0.00') I 0 O.oo~o U 0.002 U 0.002')
Cachil.lll (Cd) 0.0050 0.00')0 U 0.01 I 0 0.0050 U 0.00' U 0.0025
Calcil.lll (Ca) O. 1500 85.9230 HS 2 0 ill ~ ~
CniUII (Cs) 0.0200 1.0000 U 1.0 0 0 .......
ChrOllliUII (Cr) 0.0100 0.0100 U 0.0') 2 0 0.0100 U 0.01 U 0.0050
Cobalt (Co) 0.0220 O.OSOO U 0.0') 2 ° 0.0220 U 0.020 U 0.0110
Copper (Cu) 0.0063 0.0250 U 0.2 2 0 0.0063 U 0.020 U 0 . 0032
Iron (Fe) 0.0069 I. 7800 " 0.3 2 0 0.062 0.062 0.0327
Lead (Pb) 0.0050 0.0055 . 0.05 I 0 0.005 0.00') 0.0050
li th iUII (li) 0.1000 0.1000 U 2.5 0 0 .......
Hegnes iUII (Hg) 0.0500 12.8150 HS 2 0 3'.0 32.2 --»
Hanganese (....) 0.0051 0.3680 . 0.05 2 2 0."2 + 0.393 + ~+
Hercury (Hg) 0.0002 0.0003 . 0.002 I 0 0.0002 U 0.0002 U 0.0001
Hol ybdenum(Ho) 0.0220 0.1000 U o. I I 0 0.0220 U 0.0' U 0.0110
Hickel (Hi) 0.0310 0.0'00 U 0.20 2 0 0.0310 U 0.020 U 0.0185
Potass h.. (K) 0 . 5000 5.0000 U HS I 0 I.~' 1.5' I .5'00
SehniUII (Sa) 0.0050 0.0050 U 0.01 I 0 0.0050 U 0.005 U 0.0025
Silver (Ag) 0 . 0016 0.0100 U 0.05 2 0 0.0016 U 0.01 U 0.0038
SodiUII (Ha) 2. 1000 '6.2'')0 HS 2 0 ill 102 106
Stront il.lll (Sr) 0.0200 0.3960 HS 2 0 1.Z5 TJi1 Ti6iiO
ThalliUII (Tt) 0.0100 0.0100 U O.OIU 1 0 mOO U iOOo U + ""iiJiiM
Tin (Sn) 0.1000 0.1000 U O. I 0 0 .......
Vanad i UII (V) 0.02'0 0.0')00 U O. I 2 0 0.02'0 U 0.010 U 0.0120
Zinc (In) 0.0200 0.0320 " 2.0 2 0 0.03 0.028 0.0290
(+) Value exceeds ARAR; ( ) Valua exceads background; , - Value shovn is TBC; "Vhere no Tolarance Interval. highest background value.
..The averaga is computed by first deter~ining tha arithn.tic ~an concentration at Individual valla/stations and then using this date to
compute tha arlth.etlc mean for the veils/stations In this group. If. datUII Indlc.tes non-detected. the value used in computation of
the arithmetic mean is one-half the Contract Requlrad Datectlon LI.lt (CRDL)....
HS-HO Standard. U-Oatactlon LI.it. J-Presant balow Detection LI.lt. B-Prasant in Blank.
Hini~. Hexi_. and Averaga basad on all .vailable d.t..
Veils/Stations in this group: SV063
-------
.. .
~
..
STATION 103
DISSOLVED METAL CONSTITUENT CONCENTRATIONS
IN SURFACE WATER
ALL CONCENTRATIONS IN 8q/l
Detect Ion B.ckground ARAR """er of """er of Results H.x I:"" Hlnl- Av.r8g. of'"
An.lyte limit". Valu.. V.lue Rnul ts Abov. ARAR V.lue Valu. AU Valun
Alumlnull (AI) 0.0290 0.'850 . 5.0 6 0 0.035 .0300 U 0.0179
Ant I!IIOnY (Sb) 0.0600 0.0600 U 0.06U 6 0 0.0600 U .0600 U 0.0300
Arsenic (As) 0.0100 0.0100 U 0.25U 6 0 0.0100 U 0.002 U 0.0050
B.ri Un! (88) 0.0100 0.2800 U 1.0 6 0 .200 .151 0.0890
Beryllium (B.) 0.0050 0.0050 U 0.005 6 0 O.DOSO U 0.002 U 0.0025
Cachh.. (Cd) 0.0050 0.0050 U 0.01 6 0 0.0050 U 0.00' U 0.0025
Calc h.. (C.) 0.1500 85.9230 HS 6 0 ill 99.6 --1!!
CeslUII (Cs) 0.0200 I. 0000 U 1.0 5 0 0.0200 U .0010 U 0.0100
ChrOllllum (Cr) 0.0100 0.0100 U 0.05 6 0 0.0100 U .0100 U 0.0050
Cobalt (Co) 0.0220 0.0500 U 0.05 6 0 0.0220 U 0.020 U 0.0110
Copper (Cu) 0.0063 0.0250 U 0.2 6 0 0.0063 U 0.020 U 0.0032
Iron (Fe) 0.0069 I. 1800 . 0.3 6 0 .156 0.061 0.0521
Lead (Pb) 0.0050 0.0055 . 0.05 6 0 0.0050 U .0020 U 0.0025
LithlUII (Li) 0.1000 0.1000 U 2.5 5 0 .0160 .0100 U 0."32
MeVln i UII (Hg) 0.0500 12.8150 HS 6 0 12.60 5 U 9.9108
Heng.nn. (ft1) 0.0051 0.3680 . 0.05 6 2 .0130 + 0.010 U 0.0355
Mercury (Hg) 0.0002 0.0003 . 0.002 6 0 ~ 0.0002 U 0.0003
Holybdenull(Ho) 0.0220 0.1000 U 0.1 5 0 0.0220 U .0100 U 0.0110
Hickel (Hi) 0.0310 0."00 U 0.20 6 0 0.0310 U 0.020 U 0.0185
Pot an ium (K) 0.5000 5.0000 U HS 6 0 0.853 .5n O. "00
Selenium (S.) 0.0050 0.0050 U 0.01 6 0 0.0050 U .0020 U 0.0025
Sit ver (Ag) 0.0016 0.0100 U 0.05 6 0 0.0016 U .0100 U 0.0038
Sodium (N.) 2.1000 ".2'50 NS 6 0 ".20 5 U 11
Stroot iUII (Sr) 0.0200 0.3960 NS 6 0 ...ill 0.395 0.2110
Thall h.. (TI) 0.0100 0.0100 U O.OIU 6 0 0.0100 U .0030 U 0.0050
Tin (50) 0.1000 0.1000 U 0.1 5 0 0.1000 U .100 U 0.0500
Vaned II... (V) 0.02'0 0.0500 U 0.1 6 0 0.02" U 0.010 U 0.0120
Zinc (In) 0.0200 0.0320 . 2.0 6 0 .0270 .0200 U 0.0152
(t) V.lue .xceeds ARAR; ( ) V.lue .xceeds background; , - V.lue shown I. TBe; .Vher. no Toteranc. Interval. highe.t b.ckground value.
..Th. aver.oa II computed ~Irlt deter~lning the arlt~etic ..en concentration at Indlviduat w.lt./lt.tlon. and th.n ullng thll data to
compute the .rith..tlc ..en for the welt.l.tatlon. In thll group. If. datUII Indicat.. non-det.cted. the v.tue u.ed in computation of
the .rith.-tlc meen Is on.-h.lf the Contr.ct R.quired Detection Li.lt (CRDl)....
NS-No Stand.rd. U-Oetectlon LI.it. J-Pre..nt b.low O.tectlon ll.lt. B-Pr.sent in Blenk.
Hinl_. "'xi_. end Aver8ge ba..d on all av.II.a. dau.
-------
STATION 103
DISSOLVED METAL CONSTITUENT CONCENTRATIONS
IN SURFACE WATER
ALL CONCENTRATIONS IN mq/l
Detection B.ckg"ound ARAR ~er 0' Numbe" 0' Results Hex ilIUm "Inl- Ave".e 0' u
An. I yte Limit." V.lus. V.lue Resul ts Above ARAR V.lue V.lue All V.lues
A 11....1 null (AI) 0.0290 0.48!»0 .. S.O 6 0 O.OJ!» .0300 U 0.0179
Ant l.ony (Sb) 0.0600 0.0'00 U 0.06U 6 0 0.0600 U .0600 U 0.0300
A"senlc (As) 0.0100 0.0100 U 0.25U 6 0 0.0100 U 0.002 U 0.0050
B." h... (88) 0.0100 0.2800 U 1.0 6 0 .200 .151 0.0890
Be"yl! h... (Be) 0.0050 0.0050 U 0.005 6 0 0.0050 U 0.002 U 0.0025
C.diR h.. (Cd) 0.0050 0.0050 U 0.01 6 0 0.0050 U 0.00' U 0.0025
C.lc h.. (C.) 0.7500 85.9230 NS 6 0 ill !L.! --1.!!
Ce.lln (Cs) 0.0200 1. 0000 U 1.0 5 0 0.0200 U .0010 U 0.0100
Chr_ium (Cr) 0.0100 0.0100 U 0.05 6 0 0.0100 U .0100 U 0.0050
C0b81 t (Co) 0.0220 0.0500 U 0.05 6 0 0.0220 U 0.020 U 0.0110
Coppe" (Cu) 0.0063 0.0250 U 0.2 6 0 0.0063 U 0.020 U 0.0032
I"on (Fe) 0.0069 1. 7800 .. 0.3 6 0 .156 0.061 0.0521
L..d (Pb) 0.0050 0.0055 .. 0.05 , 0 0.0050 U .0020 U 0.0025
li th I UIII (li) 0.1000 0.1000 U 2.5 5 0 .0160 .0100 U 0.0'12
Hegnes I UIII (Hg) 0.0500 12.8150 NS 6 0 12.60 5 U 9.9708
Hengenen (tt-!) 0 . 005 1 0.3680 .. 0.05 , 2 .0730 + 0.010 U 0.0355
Hercury (Hg) 0.0002 0.0003 .. 0.002 6 0 .0007 0.0002 U 0.0003
Holybdenull(Ho) 0.0220 0.1000 U 0.1 5 0 0.0220 U .0100 U 0.0110
Nickel (HI) 0.0370 0."00 U 0.20 , 0 0.0370 U 0.020 U 0.0185
Pot.n iUIII (I() 0.5000 5.0000 U NS 6 0 0.853 .5" 0.'000
Selenium (58) 0.0050 0.0050 U 0.01 , 0 0.0050 U .0020 U 0.0025
S II ve" (Ag) 0.0016 0.0100 U 0.05 6 0 0.0076 U .0100 U 0.0038
SodiUII (He) 2.1000 ".2'50 HS 6 0 ".20 5 U 11
St"ont iUII (Sr) 0.0200 0.3960 NS , 0 ..m 0.395 0.2110
Theil iUli (TI) 0.0100 0.0100 U O.OIU 6 0 0.0100 U .0030 U 0.0050
Tin (Sn) 0.1000 0.1000 U 0.1 5 0 0.1000 U .100 U 0.0500
V8n8d iUII (V) 0.02'0 0.0500 U 0.1 , 0 0.0240 U 0.010 U 0.0120
Zinc (In) 0.0200 0.0320 .. 2.0 , 0 .0270 .0200 U 0.0152
(t) V.lue exceeds ARAR; (----) V.lue exceeds b.ckg"ound; ,- V.lue shown Is TBC; .Vhere no Tolerenee Interv.l. highest backg"ound v.lue.
".The .ve".e Is computed by 'I"st dete".inlng the arlth.etlc ..en concent".tion at Indivlduel vell./.t.tlons and then using this date to
compute the ."ith.8tlc ..en '0" the vells/st.tlons In this group. I'. datUIII Indic.tas non-detected. the value used In c~t.tion 0'
the ."Ithmetic maen Is one-hel' the Cont".ct Required Detection LI.lt (CROL)..".
HS-No Standa"d. U-Oet.ctlon Li.lt. J-Pre.ant belov Detection LI.lt. B-P"esent in Blank.
Hinl_. "'xl_. end Ave".e based on .ll .vailable dat..
Uells/Stations in this g"oup: SU103
-------
..
:to
..,
STATION 53
TOTAL METAL CONSTITUENT CONCENTRATIONS
IN SURFACE WATER
ALL CONCENTRATIONS IN 89/1
Oetection Background ARAR ~er o' ~er 0' Results Hax;- Hini.... Avaraga o,u
Analyte Limit"" Vatue" Vetue Ruut ts Above ARAR Vetue Vetue Att Vetues
Atuminum (At) O. 2000 0.9160 " 0.2U 6 , 6.62 . .200 U 1. 7060 .
Ant i",ooy (Sb) 0.0600 0.0400 U 0.061,UI 6 0 D.06OO U .01,0 U 0.0]00
Arsenic (As) 0.0100 0.0100 U 0.05 6 0 0.0100 U .010 U 0.0050
Barium (Be) 0.2000 0.2000 U 1.0 6 0 .U8 .218 ..llill
Berylt ium (Be) 0.0050 0.0050 U O. I 6 0 .0055 .005 U 0.0030
CechiUIII (Cd) 0.0050 0.0050 U 0.01 6 0 0.0050 U .005 U 0.0025
Celcium (Ce) 5.0000 85.0080 6 0 U6 116 ----ill
Cuium (Cs) 1.0000 I. 0000 U I. OUt 5 0 f.1jooou :100 U 0.5000
ChrOMium (Cr) 0.0100 0.0100 U 0.05 6 0 0.0100 U .010 U 0.0050
Cobet t (Co) 0.0500 0.0500 U 0.05U 6 0 0.0500 U .050 U 0.0250
Copper (Cu) 0.0250 0.0250 U 0.2 6 0 .0299 .025 U 0.015'
Iron (Fe) 0.1000 3. 1670 1.0 6 6 22.30 . 5.06 . 8.8'00 .
Lead (Pb) 0.0050 0.0050 U 0.05 7 I .0623 . .0030 U 0.0110
Lithium (Li) 0.1000 0.1000 U 2.5 5 0 .021,0 .02'0 0.OU8
Hegnu ium (Hg) 5.0000 12.'800 6 0 ~ 2'.60 --ll
Hengenue (tt\) 0.0150 0.6360 1.0 6 0 .719 ."7 0.5873
Hercury (Ifg) 0.0002 0.0010 0.002 6 0 .0007 .0002 U 0.0002
Hotybd8num(Ho) 0.1000 0.1000 U 0.1 5 0 0.1000 U .0100 U 0.0500
Hicket (Hi) 0.0'00 0.01,00 U 0.2 6 0 0.0'00 U .01,0 U 0.0200
Potessium (K) 5.0000 5.0000 U 6 0 5.0000 U 5 U 2.5000
Setenium (Se) 0.0050 0.0050 U 0.01 6 0 0.0050 U .005 U 0.0025
5 it ver (Ag) 0.0100 0.0106 " 0.05 6 0 0.0100 U .010 U 0.0050
Sodium (He) 5.0000 1,1 . 3620 6 0 20.90 ".70 18
Stront ium (Sr) 0.2000 0.3820 HS 6 0 .8" .796 .Jh!ill
Thelt ium (Tt) 0.0100 0.0500 U 0.05U 6 0 OJiioo U .010 U 0.0050
Tin (50) 0.2000 0.1000 U 0.1U 5 1 .109 + .100 U 0.1018 .
Vanadium (V) 0 . 0500 0.0500 U 0.1 6 0 if.'ijf«jij U .050 U "'iI.Offii
Zinc (In) 0.0200 0.0276 2.0 6 0 ..R! .0200 U ~
(t) Vetue exceeds ARAR; ( ) Velue exceeds background; ,- Vetue shown i. TBC; "Uhera no Toteranca Intarvel. highest background vetue.
..'he .varage is c~ted by 'irst deter.ining the .rit~tic ..an concentr.tion et individUat vetta/.t.tion. end then u.ing this date to
c~te the arit~tic ....an 'or the vetts/st.tions in this group. I'. datu. indic.tes non-detacted. the v.tue used in c~t.tion 0'
the erlth..tlc meen is one-het. the Contr.ct Required Oetection Li.it (CRDL)""".
HS-Ho Stenderd. U~etectlon Li.it. J-Pre.ent betov Detection Li.it. B-Pre.ent in Btenk.
Hini_. Haxi_. end Average b.sed on .tl .v.ilable dat..
-------
. .
SOUTH WALNUT CREEK
TOTAL METAL CONSTITUENT CONCENTRATIONS
IN SURPACE WATER
ALL CONCENTRATIONS IN 89/1
Detect Ion B.ckgrou.d ARAR ~er 0' ~er 0' Results HeKI- Hlnl- Aver.g. 0'--
An.1 yte limit-" V.tu.- V.lue Results Abov. ARAR V.lue V.lue All V.lues
Alumlnull (AI) 0 . 2000 0.9160 - 0.2U 21 " 2S.'0 + .0300 U ..L.!!ll +
An t I IIIDnY (Sb) 0.0600 O.O~OO U ° . 06"" 21 ° :o6i"I 0.060 U 0.0309
Arsenic (As) 0.0100 0.0100 U O.O~ 21 ° iiJi100 U .0020 U O.OO~O
B.ri- (B.) 0.2000 0.2000 U 1.0 21 1 ~ .110 0.2330
Beryl! lum (B.) 0.0050 0.0050 U 0.1 21 ° .0572 .0020 U ..!.!ill
C.chl- (Cd) 0.0050 0.0050 U 0.01 21 I .01(2 + .00'0 U 0.0030
Cetclum (Ce) 5.0000 85.0080 21 0 ill 7.73 80
Cesium (Cs) 1. 0000 1. 0000 U LOllI 23 0 1. 0000 U .0010 U 0.5000
Chromium (Cr) 0.0100 0.0100 U 0.05 27 I .212 + 0.010 U ..!J!ill
Cobelt (Co) 0.0500 0.0500 U O.OSU 21 I .132 + .0200 U 0.0295
Copper (Cu) 0.02S0 0.02S0 U 0.2 21 I .293 + .0200 U 0.0271
Iron (Fe) 0.1000 3. 1610 1.0 21 12 20' + .08S5 12 +
teed (Pb) O.OOSO O.OOSO U O.OS 27 I .21~ + .0020 U 0.01'0
li th iUII (li) 0.1000 0.1000 U 2.S 23 0 .IS2 .0100 U 0.OS33
Megnesh.... (Hg) 5.0000 12.'800 21 0 ]6.70 S.O U "
Hengenese (..,) O.OISO '0.6]60 1.0 21 I r68+ .0100 U T360j
Mercury (Hg) 0.0002 0.0010 0.002 21 1 .002' + 0.0002 U 0.0002
Holybd8nu11(Ho) 0.1000 0.1000 U O. I 23 I .IU + .0100 U 0.OS61
Nicket (Ni) 0.0'00 0.0'00 U 0.2 21 I .2" + .0200 U 0.02"
Poten ium (I() 5.0000 5.0000 U 21 0 21.50 .62' ].322'
Selenium (58) 0.0050 0.0050 U 0.01 21 ° .00S9 .0020 U 0.0026
Silver (Ag) 0.0100 0.0106 - 0.05 21 0 .0117 0.010 U 0.0053
Sodium (He) S.OOOO '7.3620 21 0 58.20 S U 29
Stront ium (Sr) 0.2000 0.3820 HS 21 0 0.8 .100 U 0.2311
Theil ium (11) 0.0100 O.OSOO U 0.05U 21 0 if.ii I 00 U .00]0 U 0.0050
Tin (Sn) 0.2000 0.1000 U O.IU 2] ° 0.2000 U .100 U 0.1000
Venlld I um (V) 0.0500 0.0500 U 0.1 21 1 ~ .0100 U 0.0'99
Zinc (In) 0.0200 0.0216 2.0 21 0 L..!! .0200 U 0.2363
(+) Velue eKceeds ARAR;.( ) Vetue .Kceeds beckground; , - Velue shown Is TBC; -Vher. no Toterence Intervel. highest beckground velue.
-.'he .verege Is cOMpUted by 'Irst determining th. .rithMetlc ..en concentr.tlon .t Indivlduet v.lts/stetions end then using this dete to
compute the erlth.-tlc ..en for the vetts/st.tlons In this group. I'. detUil Indlcetes non-detected, the velue used in c~tetion 0'
the erithmetlc meen Is one-h.I' the Contrect Required Detection limit (CRDl)-...
HS-Ho Stenderd. U-Oetectlon limit. J-Pre.ent b.tov Oetection li.it. B-Present in Blenk.
Hini~. He.i~. end Averege besed on .It evelleble det..
Vells/Stetlons In this group: SV056. SV060. SV061. SVIOI
~
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'.,
..
..
STATION 59
TOTAL METAL CONSTITUENT CONCENTRATIONS
IN SURFACE WATER
ALL CONCENTRATIONS IN aq/1
Oeuction B.ckground ARAR tUIIb.r 0' tUIIb.r 0' R.sults Hex i;"" "Ini- Av.reg. 0'..
An.lyu limit." V.I.u,. Velu. Ruul ts Abov. ARAR V.lu. V.lu. AU V.luu
Ahn i null (AI) 0.2000 0.9160 . 0.2U 1 S ~ .190 6.6900 +
Ant IIIIDnY (Sb) 0.0600 0.0600 U 0.06'01 1 1 .:.1R.! 0.060 U 0Jiiiij
Arsenic (As) 0.0100 0.0100 U O.OS 1 0 0.0100 U .0020 U O.OOSO
B.ri 1ft (B.) 0.2000 0.2000 U 1.0 1 0 ."1 . 166 0 . 20"
B.ryl I ilft (B.) O. OOSO O.ooSO U 0.1 1 0 :0016 .0020 U 0.00.J1
Cech"... (Cd) O.OOSO O.ooSO U 0.01 1 0 ii:iiOSo U .00'0 U 0.002S
C.lcium (Ce) S.OOOO 8S.OD80 1 0 "6 102 183
Cuium (Cs) 1.0000 1. 0000 U 1. 001 6 0 i:Oooo U .0010 U TIiiiiO
Chromium (Cr) 0.0100 0.0100 U O.OS 1 0 .0232 0.010 U 0.0090
Cob.1 t (Co) O.OSoo O.OSOO U O.OSU 1 0 O.OSOO U .0200 U 0.02S0
Copper (Cu) 0.02S0 0.02S0 U 0.2 1 0 ,OU6 .0200 U 0.021S
Iron (Fe) 0.1000 3.1610 1.0 1 , 11+ .100 U S.18S1 +
t..d (Ph) O.OOSO O.OOSO U O.OS 1 0 :on 1 .0020 U lI.'iiffi
Li thi.... (li) 0.1000 O. 1000 U 2.S 6 1 2.S6 + .02S0 0."08
Hegnu"", (Hg) S.OOOO 12.'800 1 0 28.10 20.60 -g
Hengen. se (....) 0.01S0 0.6360 1.0 1 0 -:m- .0100 U 0.0123
Mercury (He) 0.0002 0.0010 0.002 1 0 .0006 0.0002 U 0.0002
Holybdenum(Ho) 0.1000 0.1000 U 0.1 6 0 .0191 .0191 0.OU9
Nickel (Ni) 0.0'00 0.0'00 U 0.2 1 0 0.0'00 U .0200 U 0.0200
Pot.ss ium (K) S.OOOO S.ooOO U 1 0 .819 .819 2.2S99
Selenium (Se) O.OOSO O.ooSO U 0.01 1 1 .0160 + .0020 U O.OOU
Sit v.r (Ag) 0.0100 0.0106 . O.OS 1 0 0.0100 U 0.010 U O.OOSO
Sodium (N.) S.OOOO ".3620 1 0 .J1 . 60 29 33
Strontium (Sr) 0.2000 0.3820 NS 1 0 1.36 ,601 O. 6096
Th.llium (It) 0.0100 O.OSOO U 0.05U 1 0 WOO U .0030 U li:'iiimj
Tin (Sn) 0.2000 0.1000 U 0.10 6 0 0.2000 U .100 U 0.1000
V...ed il.lll (V) O.OSOO 0.0500 U 0.1 1 0 ...DID .0100 U 0.03"
line (In) 0.0200 0.0216 2.0 1 1 2.66 + .209 0.81'1
(+) V.lu. .xce.ds ARAR; <----) Velu. .xceeds b.ckground; ,- V.lu. .hown is TBe; .Wh.re no Tot.renee Interv.t, highe.t beckground v.lue.
..The .v.rege is c~t.d by 'ir.t d.t.r.ining the .rithmetic ..... concentretlon .t Indivldu.t v.tt./.tetlon. end th.n u.ing thl. det. to
compute the .rithMetic ..... 'or the v.tts/.t.tion. In thie group. I' e detu. Indicete. non-det.cted. the vetu. used in co.putetlon 0'
the erlthMetic ..... Is on.-h.t' the Contr.ct R.qulr.d Detection ll.lt (CROl)....
NS-No Stend8rd. U-O.tectlon ll.it. J-Preeent b.lov Detection ll.lt. B-Pr.sent In Blenk.
"ini_. Hexi_. end Averege bend on ell ev.llebt. dete.
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':. ~
STATION 63
TOTAL MeTAL CONSTITUENT CONCENTRATIONS
IN SURI'ACE WATER
ALL CONCBNTRATIONS IN 8q/l
Detection eeckground ARAR tb.ber 0' tb.ber 0' Results "'~i- "ini- Aver...e o'u
Anel yh li",it". VeLue. Velue Resulu Above ARAR Velue Velue All Velues
Alurnil'Ull (AI) 0.2000 0.9160 . 0.2U I 1 O. 7~0 + 0.7~0 + 0.7~00 +
Ant imony (Sb) 0.0600 0.0600 U O. "'Ill I 0 0.0600 U 0.500 U + 0.0300
Arsenic (As) 0.0100 0.0100 U 0.05 I 0 0.003 0.003 0.0030
eeriurn (Be) 0.2000 O.tooo U 1.0 I 0 0.107 0.107 0.1070
eeryl! lurn (ee) o.oo~o 0.0050 U 0.1 I 0 0.0050 U 0.002 U 0.0025
Cech II.. (Cd) 0.0050 0.0050 U 0.01 I 0 0.0050 U 0.00' U 0.0025
Cel c i.... (Ce) 5.0000 85.0080 I 0 !U ~ --U
Cesi.... (Cs) 1.0000 1.0000 U 1.0IlI 0 0 .......
ChrOlllI.... (Cr) 0.0100 0.0100 U 0.05 I 0 0.0100 U 0.020 U 0.0050
Cobel t (Co) 0.0500 O.OSOD U 0.05U I 0 0.0500 U 0.020 U 0.0250
Copper (Cu) 0.0250 0.0250 U 0.2 I 0 0.02SO U 0.020 U 0.0125
Iron (Fe) 0.1000 3.1670 1.0 I I I. 32 + 1.32 + 1.3200 +
Leed (Pb) 0.0050 0.0050 U 0.05 I 0 0.006 JW!2! 0.0060
II th i.... (lI) 0.1000 0.1000 U 2.5 0 0 ~
Hegnes i UII (Hg) 5.0000 I.U800 1 0 32.0 &it 32
Hengene58 (Hn) 0.01~0 0.6360 1.0 I 0 0."5 0."5 TmO
Hercury (Kg) 0.0002 0.0010 0.002 I 0 0.0002 U 0.0002 U 0.0001
Hol ybdenurn(Ho) 0.1000 0.1000 U 0.1 0 0 .......
Nickel (Ni) O. "00 0.0'10 U 0.2 I 0 0."00 U 0.020 U 0.0200
Pot en i.... (K) 5.0000 5.0000 U I 0 1.61 1.61 I. 6100
Seleniun (Se) O.OO~O 0.0050 U 0.01 I I !Will...! ~ 0.0110 +
Sit ver (Ag) 0.0100 0.0106 . 0.05 I 0 0.0100 U 0.030 U o:iiOSii
SodiUli (He) 5.0000 ".3620 I 0 !L! !L! 98'
Strontlun (Sr) 0.2000 0.3820 NS I 0 1.25 1.25 --.:BOO
Theil lurn (11) 0.0100 0.0500 U 0.05U I 0 0.0100 U 0.300 U + 0.0050
Tin (Sn) 0.2000 0.1000 U O.IU 0 0 ...A..-
Vened i urn (V) 0.0500 0.0500 U 0.1 I 0 0.0500 U 0.010 U 0.0250
Zinc (In) 0.0200 0.0276 2.0 I 0 0.0200 U 0.020 U 0.0100
(+) Velue exceeds ARAR; ( ) Velue exceeds beckground; , - Velue shown i. TBC; .Uhere no Tolerence Intervel. highest beckground value.
..'he .verege is co.puted by 'irst deter.ining the erithmetlc "80 concentr.tion .t indivldu.1 vette/st.tlons end then uelng this dat. to
co.pute the erith.etic ..en 'or the wetts/stetions in this group. I'. detUM Indicate. non-detected. the v.tue used In comput.tlon 0'
the .rlthmetlc "'e8O is one-hel' the Contrect Required Detection Limit (CRDl)....
NS-No Stenderd. U-Detectlon LiMit. J-Present betov Detection Li",it. B-Present in elenk.
"ini_. Haxi_. end Average b.sed on .tt eveilable deta.
Uells/St.tions in this group: SU063
~
-------
.. ..
..,
"I
,
STATION '4
TOTAL METAL CONSTITUENT CONCENTRATIONS
IN SURFACB WATER
ALL CONCENTRATIONS IN 8q/l
DeUct ion Background MAR Humber 0' Humber 0' Results HeKi- "ini- Avaraga o,u
Anal yh lillli t.'" Value. Vatua Resul ts Above ARAR Value V.lue AU Vatues
Atuni.... (At) 0.2000 0.9160 . 0.2U ] 3 15.( + ."6 + 5.61(7 .
Antimony .(Sb) 0.0600 0.~6oo U 0.0"01 ] 0 iJ.ii6iiii U .0600 U 0.0300
Arsenic (As) 0.0100 0.0100 U 0.05 3 0 0.006 0.006 0.0053
Bariun (Oa) 0.2000 0.2000 U 1.0 3 0 0.268 .200 U 0.1560
Berytlium (Oe) 0.0050 0.0050 U 0.1 3 0 0.0050 U 0.002 U 0.0025
CadMiua (Cd) 0.0050 0.0050 U 0.01 3 0 0.007 .0050 U 0.00'0
Catci..... (Ca) 5.0000 85.0080 3 0 IT6 68.50 ~
C..ium (C.) 1. 0000 1. 0000 U 1. OUt 2 0 1.'""0000 U .100 U 0.5000
ChrOlllI..... (Cr) 0.0100 0.0100 U 0.05 3 0 0.0" .0100 U 0.0170
Cobat t (Co) 0.0500 0.0500 U 0.05U 3 0 0.0500 U 0.020 U 0.0250
Copper (Cu) 0.0250 0.0250 U 0.2 3 0 0.0" .0250 U 0.0220
Iron (Fe) 0.1000 3.1610 1.0 3 2 17.1 . .920 6.3633 +
Lead (Pb) 0.0050 0.0050 U 0.05 ] 0 0.0050 U O.OO( U "1iliOZS
lithi..... (li) 0.1000 0.1000 U 2.5 2 0 .0925 .0925 0.0113
Hegnesi..... (fig) 5.0000 12.'800 3 0 56.7 ".80 -&
Hengenue (...) 0.0150 0.6360 1.0 3 0 0.368 .0515 0.1519
Hercury (Itg) 0.0002 0 . 0010 0.002 3 0 0.0002 U 0.0002 U 0.0001
Hotybdenun(Ho) 0.1000 0.1000 U 0.1 2 0 0.1000 U .0100 U 0.0500
Nicht (Hi) 0.0(00 0.0(00 U 0.2 3 0 0.023 0.023 0.0210
Po ten lun (I() 5.0000 5.0000 U 3 0 3.'2 3.(2 2.8067
Seleniun (Se) 0.0050 0.0050 U 0.01 3 1 .0115 + .0050 U 0.0055
Sitver (Ag) 0.0100 0.0106 . 0.05 3 0 0.0100 U .0100 U 0.0050
Sodiun (He) 5.0000 '1.3620 ] 0 110 99.]0 105
Stroot iun (Sr) 0.2000 0.3820 HS ] 0 1.16 .Ll! TIm
Thel t iun (ft) 0.0100 0.0500 U 0.05U ] 0 o.iiioo U .0100 U o:iiiffii
Tin (50) 0.2000 0.1000 U O.IU 2 0 0.2000 U .100 U O. 1000
Vanadium (V) 0 . 0500 0.0500 U 0.1 ] 0 o.on 0.03] 0.0217
Zinc (In) 0.0200 0.0276 2.0 ] 0 !L..ll! .0200 U 0.0113
(+) Vatue aKceeds MAR; ( ) Value aKcead. background; , - V.tue ahovn i. TBC; .Uhera no Toterenca Interv.I, highe.t b.ckground vatue.
..The .verage ia c~ted by 'irat detarmining the arit~tic ..en concentr.tlon at individual watt.l.t.tion. and then uaing this data to
c~te the arit~tic ..en 'or the wetts/.tation. In this group. I'. datun Indicates non-detected, the v.lue used in computation 0'
the arlt~tic lIIIen i. ona-hal' the Contr.ct Required Detection Limit (CRDl)....
NS-Ho Standard. U-Oetection Limit. J-Pr.sent bet ow Datactlon Li.lt. B-Pre.ent in Otank.
"inl_, HaKi~, and Average ba.ed on .tl av.itabte dat..
-------
. ,
STATION 103
TOTAL METAL CONSTITUENT CONCENTRATIONS
IN SURPACB WATER
ALL CONCBNTRATIONS IN .q/l
Detect ion 8.ckO"ound ARAR Nutite" 01 Nutite" 01 Results ...;i- . "ini- A"e"...e 0'..
An.lyte Limit." V.lu.. V.lu. Ruul h Abo"e ARAR V.lu. V.lu. All V.lu.s
AIUlli,.. (AI) 0 . 2000 0.9160 . 0.2U 6 6 169 + 0.766 + 36 +
Ant ilnony (Sb) 0 . 0600 0.0600 U 0 . 06"JI 6 0 0.0600 U .0600 U 0.0300
A"s.nic (As) 0.0100 0.0100 U 0.05 6 0 .0"8 0.002 U 0.0185
B.riUII (B.) 0.2000 0.~000 U 1.0 6 1 '.23 + 0.1" ~+
B."yll iUII (B.) 0.0050 0.0050 U 0.1 6 0 ..ill! 0.002 U 0.0056
Cedllh.... (Cd) 0.0050 0.0050 U 0.01 6 1 ~ 0.00' U 0.0061
C.lciUII (C.) 5.0000 85.0080 6 0 !!!1 99.0 309
C..iUII (Cs) 1.0000 1.0000 U 1.001 5 1 1.11+ .0010 U T6ffi
Ch"OI8IU111 (C,,) 0.0100 0.0100 U 0.05 6 1 .172 + .0100 U 0.0'10
Cob.1 t (Co) 0.0500 0.0500 U 0.05U 6 1 ~ 0.020 U ~+
Coppe" (Cu) 0.0250 0.0250 U 0.2 6 1 .213 + 0.020 U 0.0650
I"on (Fe) 0.1000 :S.1610 1.0 6 5 1'2 + 0.691 '0 +
L..d (fib) 0.0050 0.0050 U 0.05 6 3 .656 + 0.005 ""'iJ.15Zi +
Li th iUII (Li) 0.1000 0.1000 U 2.5 5 0 ~ .0180 0.0568
Hegnu I UIII (Hg) 5.0000 12.'800 6 0 56.80 5 U 19
Hengen..e (Hn) 0.0150 0.6360 1.0 6 3 'iiOO + 0.019 2.1192 +
He"cury (Hg) 0.0002 0.0010 0.002 5 0 JjOO9 0.0002 U 0.0003
Hol ybd.I1UII(Ho) 0.1000 0.1000 U 0.1 5 1 ...l!!..! .100 U 0.0628
Hickel (Hi) 0.0'00 0.0'00 U 0.2 6 1 .213 + 0.020 U 0.0622
Pote.. lun (I() 5.0000 5.0000 U 6 0 32.70 0.928 7.5297
S.hnlUII (Se) 0.0050 0.0050 U 0.01 6 0 0.0050 U .0020 U 0.0025
Sit ver (Au) 0.0100 0.0106 . 0.05 6 0 0.0100 U .0100 U 0.0050
Sodi... (N.) 5.0000 U . 3620 6 0 20.60 5 U 13
Stront iun (Sr) 0.2000 0.3820 HS 6 0 Ll! 0.389 0.5650
ThelliUII (n) 0.0100 0.0500 U 0.05U 6 0 0.0100 U :oii3O U "If.iiiiSii
Tin (Sn) 0.2000 0.1000 U O.IU 5 0 0.2000 U .100 U 0.1000
Vened I UII (V) 0.0500 0.0500 U 0.1 6 2 ~ 0.010 U 0.12'8 +
Zinc (In) 0.0200 0.0276 2.0 6 0 .J11 0.020 U 0.2563
(+) Velu. ..c..d. ARAR; ( ) V.lu. ..c.eds b.ckg"ound; ,- Velu. shown is TBC; .Vh."e no Toler8Oc. Int.r"el, highest beckg"ound ".Iu..
..Th. .".".0. is c~t.d by 'I".t d.t.".lning the .rithmetlc ..80 conc.ntr.tion.t individual vell./st.tions end then using this det. to
co.put. the ."ith8etic ..en 'or the v.lls/at.tion. In this group. I'. det... Indic.t.s non-detected, the v.lue u.ed In c~t.tion o'
the .rithmetic ..en is one-hel' the Contr.ct Requir.d Oet.ctlon Li.it (CROL)....
HS-No Stende"d. U-oetection li.it. J-P"esent b.lov Oetection Limit. B-Present in Blenk.
"ini_, "ui_. end Averege b.nd on .11 .v.iteble det..
Vells/St.tions in this group: SVI03
.j
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.,
,.
..,
90J-PAD AND LIP SITE
INORGANIC CONSTITUENT CONCENTRATIONS
ALL CONCENTRATIONS IN MG/L
Background ARAR/TBC N~r of Number of Results MaJlinun Mini...... "Average of
Analyte ***CRDl Value* Value Resul ts Above ARAR Value Value All Values
Nitrate-Nitrite as N 5.0000 2.69 10 27 1 ~ 0.06 2.900
Chloride 5.0000 106.94 250 27 0 ill 16.9 35
Sulfate 5.0000 48.81 250 27 0 120 1.0 u 47
Total Dissolved Solids 5.0000 ; 271.15 400 27 22 790 + 332 ---!l! +
NC03- 10.0000 296.97 NS 27 0 6!m 220 --»l
(+) Value eJiceeds ARAR; ( ) Value eJiceeds background
**The average is computed by first determining the arithmetic mean concentration at individual wells/stations and then using this data to
compute the arithmetic mean for the wells/stations in this group. If a datum indicates non-detected, the value used in computation of
the arithmetic mean is one'half the Contract Required Detection limit (CRDl)***.
NS-No Standard. U-Detection limit. J-Present below Detection limit. B-Present in Blank.
Minimum, MaJlimum, and Average based on all available data.
-------
STATION 53
INOROANIC CONSTITUENT CONCENTRATIONS
ALL CONCENTRATIONS IN MOIL
Background ARAR/TBC Nllftber of Number of Results Mall,i lUll Mininun "Average of
Anelyte ".CRDl Value. Value Results Above ARAR Velue Value All Values
Nitrate-Nitrite 8S N 5.0000 2.69 10 10 0 0.17 0.05 u 2.024
Chloride 5.0000 106.94 250 10 0 170 30.6 68
Sulf8te 5.0000 ; 48.81 250 10 0 49 5 u 27
Tote I Dissolved Solids 5.0000 271.15 400 10 10 ~ 460 + -ill +
HC03- 10.0000 296.97 NS 10 0 710 370 ----!.n
(+) Value ellceeds ARAR; ( ) Value ellceeds background
..The average is computed by first determining the arithmetic mean concentration at individual wells/stations and then using this data to
compute the arithmetic mean for the wells/stations in this group. If a datum indicates non-detected, the value used in computation of
the arithmetic mean is one-half the Contract Required Detection limit (CRDl)....
NS-No Standard. U-Detection limit. J-Present below Detection limit. B-Present in Blank.
"inimum, "aximum, and Average based on all available data.
Yells/Stations in this group: SY053
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. ,
t>
SOUTH WALNUT CREEK
INORGANIC CONSTITUENT CONCENTRATIONS
ALL CONCENTRATIONS IN MGIL
BackgrOU'ld ARAR/TBC NlMtJer of Number of Results Malll...... Mini- **Average of
Analyte ***CRDl Value* Value Results Above ARAR Value Value All Values
Nitrate-Nitrite as N 5.0000 2.69 10 4J 0 Y 0.05 U ~
Chloride 5.0000 106.94 250 43 0 81 3 U 35
Sulfate 5.0000 48.81 250 43 0 74 16 43
Total Dissolved Solidi 5.0000 ; 271.15 400 43 22 3300 + 26 411 +
NC03- 10.0000 296.97 IS 43 0 540 6 ---uo
(+) Value ellceeds ARAR; ( ) Value ellceeds backgrOU'ld
**The average Is computed by first determining the arithmetic mean concentration at individual wells/stations and then using this data to
compute the arithmetic mean for the wells/stations in this group. If a datum indicates non-detected, the value used In computation of
the arithmetic mean is one-half the Contract Required Detection limit (CRDl)***.
NS-No Standard. U-Detectlon limit. J-Present below Detection limit. B.Present In Blank.
Minimum, "alll~, and Average based on all available data.
-------
'..,
Surtaae Water
Total Netals S.-pling .esults
STATION 103
5'."0" 0.'8 Cohlt C.pper Iro"
_.r S...I.~ (C.). toto I (e..). t.to I (F.). toto I
../1 ../1 ../1
.-..------ -_n_.._- --- -..- '--------
N-IOJ 07/11/88 0. OZO U 0.0'0 U 0.4'1
N-IOJ OJ/II/.. .U. A .111 . 142 .
N-IOJ os/n/.. Oot. ..ot ,.t ree.t"e.
N-IOJ 04/15/.. .0500 U v .01.1 v 00.70 V
N 10J 07/11/" .0500 U V .0Mt V 11.70 V
N-IOJ 08/01/.. .0500 U V .0874 A JI.IO I
N-IOJ 0./07/., Oot. ..ot ,.. rece'v..
N-Io) lO/OJ/89 .0200 U v .0200 U V 2.88 V
N-IOJ "/OJ/8I O. to ..ot ,.. rece'"..
N-IO' "/04/'1 Ooto ..ot ,.. rec.I...
SW.IOJ 01/../10 O.to "0' ,.. r.celved
SW-IOJ 02/1'/10 D... not ret rece've"
$V-10' 01/22/.0 0... not ret recelv."
l..~ U...- MoI"..'- Mo"I."... Moretlr, 1101....,.,,-
(P"). ..to I (U). '."1 (MI). ,... I (Mo). ,... I (He). ,.,. I (MoJ, '.'.1
..'I ../1 ../1 ../1 ..'I ..'I
--- -----.
0.001 .. 11.0 0.011 0.0001 U ..
.411 A .11' A 11.80 V 10." A ... ...4 A
.11' A .100 U A IV V J." A .0001 A .100 U A
.0141 A .100 U A IS.'O V ...1 V .0001 U . .100 U A
.108 A .100 U v 1'.80 V 1.'1 V .0001 U V .100 U V
.00" V .0180 A 11.10 V .185 v .0001 U A .500 U V
VAIU( QUAII'lrIS: HI - A...I,t. ..ot r.por'.~ U - A...I,..~ "tit ...t ~.'.et~
J - Pr.....t ".1.. ~.t.et'o" I'.'t I - Pr.....t ,.. I.a.-r...r, "I...,
~'A VAIIDAIION QUAI'I(AS: (Ho y.II~.t'o.. q...1"'.r ...dle.t.. d.'. ... ..ot b... ...I'~.t...)
. . 1101""1 tt. ".. _t f . htt.t~ ...1...
" . ..tc. .",. .... ,.. 8O-11Ga r."..
I - ReJec.... . - .cc..',~,. .'t~ .M.I'ftce'te"8;
v . .,.,,~
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.
.
". .
STATION 59
INORGANIC CONSTITUBNT CONCBNTRATIONS
ALL CONCBNTRATIONS IN MG/L
'.ckgrCMnt ARAR/TIC N~r of NuMber of Results Mall illUll Minh"'l1 "Aver.ge of
Anelyte ***CRDl V.lue* Value Resul ts Above ARAR Value Value All Values
Nitrate-Nitrite a5 N 5.0000 2.69 10 11 0 5 2.7 ~
Chloride 5.0000 106.94 250 11 0 53 27 45
Sulfate 5.0000 48.81 250 11 0 62 24.5 49
Tot.l Dissolved Solids 5.0000 ; 271.15 400 11 10 580 . 210 -m.
HCO]- 10.0000 296.97 NS 11 0 ~ R! 400
(+) Value exceeds ARAR; ( ) Value exceeds backgrCMnt
**The average is computed by first determining the arithmetic mean concentration at Individual wells/stations and then using this data to
compute the arithmetic mean for the wells/stations in this group. If a datum Indicates non-detected, the value used in computation of"
the arithmetic mean is one-half the Contract Required Detection limit (CRDl)***.
NS-No Standard. U-Detection limit. J-present below Detection limit. B-Present in Blank.
Minimum, Maximum, and Average based on all available data.
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",
STATION 63
INORGANIC CONSTITUBNT CONCBNTRATIONS
ALL CONCBNTRATIONS IN MG/L
S8ckgrCMnt ARAR/TBC NlJIIber of NUMber of Results Maxi- Mlni- **Average of
Anelyte ***CRDl V81ue* V81ue Resul ts Above ARAR Value Value All Values
I 2.69
Nitrate-Nitrite 8S N 5.0000 1D 2 0 5.0000 U 0.1 U 2.500
Chloride 5.0000 106.94 250 2 0 51 50.5 51
Sui fete 5 ~oooo : 48.81 250 2 0 m 197 -ID
Total Dissolved Solids 5.0000 271.15 400 2 2 675 + 651 + ~+
HCM- 10.0000 296.97 NS 2 0 384 ~ ---.ill
(+) Value exceeds ARAR; (----) Value exceeds background
**The average is computed by first determining the arithmetic mean concentration at individual wells/stations and then using this data to
compute the arithmetic mean for the wells/stations in this group. If a datum Indicates non-detected, the value used in computation of
the arithmetic mean is one-half the Contract Required Detection limit (CRDl)***.
NS-No Standard. U-Detection limit. J-Present below Oetectlon limit. B-Present in Blank.
Minimum, Maximum, and Average based on all available data.
~ells/Stations in this group: S~063
.
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...
STATION 64
INORGANIC CONSTITUENT CONCENTRATIONS
ALL CONCENTRATIONS IN MG/L.
BackgrOlRt ARAR/TBC Numer of Numer of Results MaKi- MinlllUll **Average of
Anelyte "*CRDl Va I ue* Value Results Above ARAR Value Value All. Values
Nitrate-Nitrite a5 N 5.0000 2.69 1D 4 0 0.2 0.05 U 1.34]
Chloride 5.0000 106.94 250 4 0 64 0.5 U 42
Sulfate 5.0000 : 48.81 250 4 0 130 4.0 U --R
Total Dissolved Solidi 5.0000 271.15 400 4 4 720 + 660 + ~+
HCO]' 10.0000 296.97 NS 4 0 580 404 ~
(+) Value ellceeds ARAR; (. ) Value exceeds backgrOlRt
**The average Is computed by first determining the arithmetic mean concentration at Individual wells/stations and then using this data to
compute the arithmetic mean for the wells/stations in this group. If a datum indicates non-detected, the value used in computation of
the arithmetic mean is one-half the Contract Required Detection limit (CRDl)***.
NS-No Standard. U-Detectlon limit. J-Present below Oetection limit. B-Present In Blank.
Minimum, Mallimum, and Average based on all available data.
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..,
STATION 103
INORGANIC CONSTITUENT CONCENTRATIONS
ALL CONCENTRATIONS IN HGIL
Background ARAR/TBC Nl8Jer of NUMber of Results Mall.l- Mlnl- --Average of
Analyte ."CRDL Value. Value Resul ts Above ARAR Value Value AU Values
Nitrate-Nitrite 8S N 5.0000 2.69 10 10 0 1.3 L.2 ~
Chloride 5.0000 106.94 250 10 0 is 31 40
Sulfate 5.0000 ; 48.81 250 10 0 68 it ----3
fotal Dissolved Solids 5.0000 211.15 400 10 8 490 + 210 406 +
MC03- 10.0000 296.91 NS 10 0 ill 251 361
(+) Value exceeds AAAR; ( ) Value exceeds background
--'he average is computed by first determining the arithmetic ~an concentration at individual wells/stations and then using this data to
compute the arithmetic mean for the wells/stations in this group. If 8 datum Indicates non-detected, the value used in computation of
the arithmetic mean is one-half the Contract Required Detection limit (CADl)---.
NS-No Standard. U-Detectlon limit. J-Present below Detection limit. S-Present in Slank.
Minimum, Maximum, and Average based on all available data.
Veils/Stations in this group: SV103
-------
",
903-PAD AHD LIP 8ITB
DISSOLVED RADIOCDBMISTRY CONCBNTRATIONS
POR SURPACB WATBR
ALL CONCBNTRATION8 IN pet/l
..
.ackgrCU1d alAi IIUllber of IIUlbar 0' lesult. "'.1- Mlnl-
Anelyte Value. Velue leluh. Above AlAI V.lue V.lue
Groll Alphe 4.3760 '7.0 5 0 LiZ < 2.00
Groa. let. 8.1980 .5.0 5 0 .28 < 4.00
Strontl.. 89, 90 1 .3980 '8.0 0 0 < 1.00
,Iutonl.. 2'9, 240 0.0000 .05 5 ) L.!t..! < 0.01
A-.rlel.. 241 0.01)0 .05 0 0 < 0.01
Irlth.. 0.0000 500 0 0
lotel Uranh.. I .8000. 5.0 5 I Lm...!. 2.860
..Awr... 0'
All V.luea
2.8
2.0
.-....
-1r..!.Q .
.......
.......
---LJ
C+) V.lue exceeds AlAI: C_) V.lue exceeds "ck,rCU1d
'"a ayer... la CClllpUted by flrat dete...lnlng tile .rlt_tlc -., concentr.tlon .t IndlylctJ81 ",II./.t.tl.. and thin ual,. thl. dIIte to
cClllpUte the arltheetlc ..an for the wella/ltatlona In thll ,r~. .,. dIIt.. Indlc.tea . 1.1. th., (c) value, or the counting error
for . d8t~ II gre.ter than the dIIt~, the y.lue used In the cClllpUt.tlon la one ".1' the Mini... Detectabl. Activity CMOA).
liS-11o Standard ."'en no 8.ckgrCU1d lolennce Interval v.lue uaed I. the Mlnl- Detectable Activity CMOA)
Mini..., Mall 1_. and Aver... bIIaed on all av.llabe dIIt..
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. ,
STATION 53
DISSOLVED RADIOCHBMISTRY CONCENTRATIONS
FOR SORWACB WATER
ALL CONCENTRATIONS IN pet/l
88Ck,rCMRt AlAI IIlJIIber of llUillMr of I..ul t. ...111- "Inl-
Anllyte V.lue. Vllue "Iul ts Above AlAI Value Value
Gross Alpha 4.3760 ,7.0 2 1 I:.!L! c 2.00
Groll letl 8.7980 5.0 2 1 7 . c 4.00
St ront lue 89. 90 1.5980 ;8.0 1 0 .0 c 1.00
Plutonlue 2)9. 240 0.0000 .05 2 Z tIP 0.20 .
A.rlclue 241 O.OUO .05 1 0 O.OJ
'rltlue 0.0000 500 0 0
10t.1 ur.niUl 1.8000* 5.0 2 I ~ 2.000
..Awrlll of
AI I Values
-H
0.50
----1d .
JdB
.-.--.-
-Y
(.) V.lue exceeds ARAI; ( ) v.lue exceeds I.ck,round
Ihe lver... I. COIIIpUted by flnt dlte...lnlng the .rlt_tlc .an concentr.tlon It Indlvlduel well./.tIU- and thin using thl. dltl to
cOIIpIte the arlt'-tlc -In for the weill/lhtlon. In thll ,roup. If I detUi Indicate. I lea. than Cc) wlue, or the ccuul", error
for . ~tUl I. ,re.ter thin the detus. the v.lue used In the cOIIpIt.tlon II one h.lf the "Inl- Oetectable Activity (MOA).
IIS-llo Standard .When no l.ck,rCMRt loler.nee Interval vllue used I. the "Inl- Detectabl. Activity (MOA)
"101-. "IX 1_. Ind Averl,e based on .11 IYlilebe det..
Uell./Stltlona In this ,roup: SU05)
-------
'H\
Il.
SOUTH WALHOT CRBBK
DISSOLVED RADIOCR8HIS~RY COHCBHTRATIONS
POR SURPACB WA~8R
ALL CONCBNTRATIOH8 IN pCl/l
Background ARAR IIUIIbe r 0' IIUllber 0' .eaul tl "alll- "Inl- . ..Aver.....o'
Analyte Vllue. Value ..sults Above OA. Value Value All Vllue.
Gross Alphl 4.3760. '7.0 II 1 It.:.t..! « 2.00 1.8
Groll leta 8.7980 5.0 8 5 UaU « 4.00 ~.
Stronth.. 89, 90 1.1980 :8.0 4 0 .1 « '"00 0.50
Plutonlua 219, 240 0.0000 .05 8 0 ...1H..! « 0.01 -
AlMlrlclua 241 0.0130 .05 4 0 L.H « 0.01
Trlth.. 0.0000 500 0 0 .......
Tot.1 Uranh.. 1. 8000. 5.0 8 5 10.260 . < 1.80 --Y
c.) Vllue eltCeeds ARAR; C_) Value uceed. Blck.round
The Iverege t. cOIIIpUted by flnt delerainlng the arlt_tlc .en concentration at Indlvl4Jat well".tatlons end then uslne thl. data to
cOIIIpUte the erlt_tlc .en 'or the ",".,.18tlonl In this .r~. If a dat'-8 Indlcete. . Ie.. then (c) Vllue, or the cOU'Itine error
'or a datua I. .reater then the dltua, the velue used In the cOMpUtltlon I. one h.I' the Mlnlaua Delect8ble Activity (NDA).
IS-No Standard .When no Beckground Tolerance Int.rval value used II the "'nl- Detecleble Activity (NDA)
"101_, "all I aua, and Average based on 811 avaHabe data.
-------
...,
STATION 5'
DISSOLVBD RADIOCRBHIS~RY CONCBNTRATIONS
POR SURPACB .ATBR
ALL CONCENTRATIONS IN pCl/l
81ckgromd AlAI 1I8tMIr of IU8bIr of I..ult. 111.'- IIlnl- . --Awr... of
Anllyte Vllue- Vllue lesul ts Above AlAI Vllue Value All Vllue.
Groas Alphl 4.3760 '1.0 2 1 l!..! 5.0J --11 *
Gro.. letl 8.7980 5.0 2 1 ..24 t < 4.00 5.' *
Stront'.. 89. 90 '.J980 ..0 1 0 0.2 < '.00 0.50
Pluton'.. 2J9. 240 0.0000 .05 Z 0 3W < 0.01 -tm
A.rlcl.. 241 o.ono .05 1 0 < 0.01
'rlt'" 0.0000 500 0 0 -......
'0181 Uraniun 1.8000. 5.0 2 2 ~ 5.660 t -ide
(t) V.lue exceed8 ARAI; ( ) Value e.ceeds lackgr"'"
'hi IV"I.e I. ClllllpUted by fint detenlin'na the arlth8ttc .... concentration It Indlvl~1 WlI&I/.tltlone end then ua'na thl. clat. to
cOIIpIte the arit-'-t Ic _en for the weU./.taUon. In thl. Ir....,. If. clat.. Indlcet.. . II" th... (c) wtUl. or the cOWIttna Irror
for I clat.. II ,relter then the det... the v.lue used In the CClllpUtltion II one hilt the IIlnl- Detect_Ie Actl"lty (MDA).
IS'No St.ndard .When no lackground 'oler.nee Inte,vII vllue uaed I. the IIlnl- Detectable Activity (MDA)
IIln'_. 1I..i_. end "ve,..e ba.ed on all .".il8be dltl.
Weili/Stationa In this .r....,: SW059
.~
-------
...,
S'I.'I108 63
DISSOLVED RADIOCRBMIS'IRY C08CBHTRATIONS
POR SURP.CB 8.'I8R
ALL CONCBN'IRATIOHS IN pCIII
'acltground AlAR IIUllber of NU8b8r of .e.ult. l18li1- Mlnl- ..Aver..,. of
Analyte Value. Value le.utt. Abov. AlAI V.lue Vatue All Vatue.
Gross Alpha 4.1760 7.0 1 1 ~ 8.25 + -L}+
Gro.. 'eta '.7980 '5.0 1 1 1L!.! 18.9 . .....11 .
StrontlUl 89, 90 1.5980 ,8.0 0 0 < 1.00
Plutonlu. 2J9, 240 0.0000 ' .05 1 0 ..mL.! c 0.01 ..Lmt
Aller Iclu. 241 0.0150 .05 0 0 c 0.01 .......
Trltltll 0.0000 500 0 0 .......
fot.1 Uranlt8 1.8000* 5.0 1 1 11.190 + 17.790 + -11+
(+) Vatue eKceedl AlAR; ( ) Value eKceeds 'acltground
'he .verage I. cClllpUted by fir.. .t.,.lnl", the .rlt""tlc _en concentr.tlon.t Indlvlul ...1I.,.t.lI- and then using thl. dlt. to
cClllpUte the .rlt_tlc _en for the well./ltatlon. In thlt group. If. .tl8 Indlnt.. . I... then (c) vel... or the count I", error
for a datu. I. greater then the dattll, the value used In the cClllpUtatlon I. one h.I' the Mlnl- Detectable Activit, (NDA).
liS-No Stendard .When no 'ackground Tolerence Interval vatue uaed I. the Mlnl- Detectable Activit, (NDA)
Mlnl_, Mnl-, and Average ba.ed on all avait.be dati.
-------
..,
8TATI0. ,.
DISSOLVED RADIOCBBHI8TRY COHCBHTRATIONS
POR SURrACB .ATa.
ALL CONCBNTRATION8 IN pCI/l
"ckgrOWld AlAR lI~r of IlUlbir of I..utt. ....a- "Inl- ..Awr818 of
An8tyle v.tue. V,!lue .esul ts Above AlAI Vatue Value All Vatues
Grosa Alpha 4.1760 ' 7.0 1 0 t:1i 6.34 -Y
GrOl. let a 8.7980 5.0 1 1 7.20 + 7.20 + 7.2 +
Stronll.. 89, 90 1.3980 :8.0 0 0 < 1.00 -....
Plutonl.. 2J9, 2'0 0.0000 .05 1 0 .00 < 0.01 -LmI
Alllerich.. 241 0.0130 .05 0 0 < 0.01 .......
Irillu. 0.0000 SOO 0 0 .......
'oUI UreniUII 1.8000. 5.0 1 1 IS.SJO + 15.530 + -1t+
(+) Value exceedS ARAI; ( ) Value exceeds 'ackgrOWld
'he average I. CClllpUted by flnt deterainlng the arlt_tlc .an concentration at Indlvlbt ...U8'8taU... ... tllen &alng thl. det. to
cOlpUt. the erith8etlc .an for Ihe welt./.tatlona In thl. ,roup. If a det.. Indicate. 8 Ie.. than ee) V81ue. or the counting error
for a clat.. I. greater than the clat.., Ihe value used In the cOIpUutlon I. one h... the "Inl- Detectable Activity (MDA).
115-110 Standard .""en no lackgrOWld 'oleranee Interval value ..ed I. the "Ini- Detectabl. Activity (MDA)
"Inl_, "axl_, .nd Aver..e baled on all avaHebe dlta.
-------
~
.,
STATION 103
DISSOLVED RADIOCHBMISTRY CONCBNTRATIONS
FOR 8URFACE WATBR
ALL CONCBNTRATIONS IN pCl/1
'.ckgrOlnd AlaR llUiber of lIumer of ...ul U ....1- "Inl- . "Aver.... of
Analyte v.lue- Value Ie.ults Above AlAI Value Value All Valuel
. 7.0 2 0 .OJ c 2.00 1.0
Gross Alpha 4.J76O
GrOll leta 8.7980 .5.0 2 1 1LL.! c 4.00 -clI+
Stronth.- 89, 90 1.5980 ' 8.0 1 0 0.2 c 1.00
Plutonlue 2J9, 240 0.0000 .05 2 0 11 c 0.01 ~
A_rlc:lue 241 0.0110 .05 1 0 c 0.01 0.0050
Trltlue 0.0000 500 0 0 .......
Total UranlUli 1.80008 5.0 2 0 4.440 J.Joo --L!
(+) Value e.ceeds ARAlli ( ) Value exceeds eack8rcud
'ha .verage la CCllllpUted by ftrlt detenlinlng the Irtth8ttc ..... concentration at Indlvlchll welli/itatione ... then uelng thll data to
cCllllpUt. the arlth.-etlc _en for the wells/statlonl In thll group. If. detue Indlcatel a 1..1 th.... (c) value. or the counting error
for a dltue Is greater th.... the detue, the value used In the cCllllpUtatlon Is one half the "Inl- Detectlble Activity (MDA).
IS-No Standard -"'en no leck8rcud Toluenee Interva' value Uled la the "Inl- Oetect.bl. Activity (MDA)
"Inl_, "a.i_. and Averege baled on 811 availebe dat..
-------
..,
Analyte
'03-PAD AND LIP 81TB
TOTAL RADIOCHBMISTRY CONCBNTRATIONS
POR SURPACE WATBR
ALL CONCBNTRATIONS IN pCl/I
8ackgromd ARAR NUlliber of NUlliber of Ra.ult. ...111- "Inl- --Aver... of
Value- Value RHul ts Above AlAR Value Value All Value.
7.7450 '7.0 13 11 »!l.! < 2.00 ----.n +
9.8880 5.0 1] 11 tU < 4.00 -.ft+
2.0400 :8.0 1] 0 ~ < 1.00 0.69
0.0180 .05 18 17 U1 < 0.01 -11+
0.0420 .05 1] 7 < 0.01 --Li +
257.18 500 18 1 ~ <400.00 230
1.8000* 5.0 18 4 18.100 + 1.770 --!.1
Groll Alpha
Groll let a
StrontlUl 89, 90
Plutonlu. 239, 240
Alllericlu. 241
Trttlu.
Total UranlUl
(+) Value exceeds ARAR; ( ) Value exceeds 8ackgromd
The a"arage la CCl8lp.lted by flrat dete,..lnlng the arlt_tlc .en concentration at Indlvl"l well.,.tetlOO8 ... then &alng thl. date to
c08pUte the arlth8etlc ..an for the ...11.,.tatlon. In thl. group. If e datu. Indlcetea 8 Ie.. then «) value, or the counting error
for a datu. I. greeter than the d8tUl, the v.lue used In tha c08pUtatlon I. one half the "Inl- Detectabl. Activity (MDA).
NS-No Standard -"'en no 8ackgromd Toterance Interval value used I. the "Inl- Detectable Act Ivlty (MDA)
"Inl_, "axl_, and Avera88 based on all avaHebe dat..
Wells/Stations In this group: SW050, SU051, SU052 , SU055, SW057, SW058, SU077
-------
'...
STATIOII 53
TOTAL RADIOCHBMISTRY COIICBNTRATIONS
FOR SURPACB WATBR
ALL CONCBNTRATIONS IN pC!/l
Analyte
leckground AlAR
Velue- V_lue
Gross Alpha
Gro18 lete
Strorul", 89. 90
Plutonl", 239. 240
A_rlcl", 241
Trltl",
'otel Urenh..
7.7450
9.8880
2.0400
0.0180
0.0420
257.18
1.8000-
07.0
5.0
; 8.0
.05
.05
500
5.0
"
II.-ber of
Inul U
Mlnl-
Value
**Awrege of
All Vel...
~r of Inulte
Above AlAI
.....-
Velue
----H1 +
7.8 +
1.3
=if:
222
-Ll+
.
(+) Velue eJlceed8 ARAR; (-) Velue ellceeds 'eckground
'h. .verege I. CCllllfJUted by flrlt detel'lllning the Irlth8tlc 881'1 concentretlon et Indlvlcbal weU./etetione end then Ullng thl. dete to
cCllllfJUt. the erlth8tlc 8en for the well./.tatlon. In thl. gr~. If I det", Indlclte. I I..e th8l'l (C) Vllue. or the counting error
for I det", I. grelter th.n the det"'. the vllue used In the cCllllfJUtltlon I. one half the Mlnl- Detectable Activity (MDA).
liS-No Standard -When no Background 'olerance Interval value Uled I. the Mlnl- Detectable Activity (MDA)
Mlnl_. M8I1i_. end Aver8ge besed on 811 eV811ebe det..
Veils/Stations In this group: SUDS3
4 ] UL! 3.2
4 3 Di < 4.00
4 0 C 1.00
5 S ~ 1. 101 +
4 3 l1..! < 0.01
5 0 lli <400.00
-------
'..\
SOUTH WALHUT CRBBK
TOTAL RADIOCHBMISTRY CONCENTRATIONS
FOR SURrACB WATBR
ALL CONCBNTRATIONS IN pcl/l
Anaayte
Iec:k,romd AIAII
Vaaue. Value
I1l8Iber of
ae.ultl
IIUlber of leauat.
Above AlAI
....1-
Value
"Inl-
Vaaue
. ..Average of
All Value.
Groll Aapha
GrOi. 'eta
StrontlUII 89, 90
pautonlUII 259, 240
AllIer IdUII 241
Trlt lUll
lotaa Urenlua
' 1.0 ZJ 12 lI2..!. 2.00 --U+
1.1450. c
9.8880 .5.0 ZJ 22 m..! c 4.00 -dt+
2.0400 '8.0 25 0 lU c 1.00
0.0180 .05 27 8 ~ c 0.01 --Lll +
0.0420 .05 21 6 L!!..! c 0.01 --LYI +
251.18 500 27 0 ~ c4oo.oo 225
1.8000* 5.0 27 " 11.100 + 1.990 --1...1 +
(+) Vaaue exceedl ARAI; ( ) Value exceecta Bec:k,r""
'h. aver..e I. COIIpUted by flnt dete...lnlng the .rlt-tlc .en concentr.tlon It Indlvl4AIi ...II./.t.tlona end then UIlng thl. data to
cOIIpUte th. arit"'tlc .en for the well./atatlon. in thl. ,roup. If I datUII indlclte. a I,.. then (c) Vltue, or the cCUltlng error
for I datUII I. ,reater then the datUII, the vllue used in th, cOIIpUtatlon I. one h.lf the "Inl- Detectable Activity (MDA).
IIS'lIo Stlndard *When no Iec:k,round Toaer.nee Interv.I value used I. the "Inl- Detectabl, Activity (MDA)
"Inl_, Mlxt_, 8nd Averege baled on aa a aVli albe data.
weaas/Statlone .In this ,roup: SW056. SW060. SW061, SW101
"
-------
'.. ~
STaTION 5'
TOTAL RADIOCBBMISTRY COKCBMTRATIONS
FOR SORwacs .aTBR
ALL COMCBMTRATIOMS 1M pC!/I
"
.
Al'I8lyte
leckground AlAI
Value* VaJue
Nulber of
lesuits
~r of le.ultl
Above AlAI
lIul-
Value
IIlnl-
Velue
**Avera... of
AI I Veluel
Gross Alpha
Groe. lete
Strontlue 89. 90
Plutonlue 259. 240
A8erlclue 241
TrltlU8
Totel UreniU8
7.7450 '7.0 5 J l1i...! < 2.00
9.8880 5.0 5 4 ~ 4
2.0400 :8.0 5 0 1.0 < 1.00
0.0180 .05 6 J Iii < 0.01
0.0420 .05 5 2 < 0.01
257.18 500 6 0 200 <400.00
1.8000* 5.0 6 5 16.600 + 0.200
--2t +
--1'i +
0.60
~+
--1..D +
200
-L!+
C+) Velue exceedl ARAR; ( ) Velue exceed. lackground
The aver... II COIIIpUted by first date,.inlng the erlt"'tlc .en concentretlon at Indlvlc1Je1 ..."./.tltlone and then using till. data to
cOlllpUte the erith8etlc ..en for the ...III/Itetiona In thl. group. If a detU8 Indicate. e Ie.. than (C) velus. or the counting error
for a datU8 I. greater then the datU8. the value used In the cOIIIpUtation I. one heU the Mlnt- Detectable Activity (MDA).
IS-81o Stenderd *""en no leck,round Tolerence Intervel value Uled I. the IIlnl- Detectable Activity CMDA)
IIlnl_. lIexl_. end Averltle based on e" avaitebe date.
-------
.. .
STATIO. &3
TOTAL RADIOCHBMISTRY COlfCBHTRATIOHS
POR SURrACB WATBR
ALL COlfCBHTRATIOlfS Ilf pCt/l
ANilyte
lackground AlAI
V.lue. V.lue
Il8ItIer 0'
lesults
IlultJer 0' I..ul t.
Above AlAI
flu 1-
Value
"'n'-
Velue
-Aver..,. 0'
All Value.
GrOll Alphe
Gro.. leta
Strontl&81 89. 90
Plutonl&81 239. 240
Allerlcl&81 241
Trltl&81
'otel Urenl&81
7.7450 '7.0 0 0
9.8880 5.0 0 0
2.0400 :'.0 0 0
0.0180 .05 1 1 Lm..! 0.242 .
0.0420 .05 0 0
257.1' 500 1 1 ~ 1100 .
1.8000. 5.0 1 1 20.500 .
.......
.......
.......
---L1! .
.......
--11!!2 .
--ll .
(+) V.lue e.ceed8 AlAI; ( ) Velue e.ceedl leckground
'he .ver.... I. c~ted by Uret dete,.'nl", the .rUIIMtlc -.en concentretlon et Indlvlul ....../.t8t1- ... then uelng thla date to
c08pUte the arltllMtlc 88en for the well./.tatlona In thla group. If. dlt&81 Indlc.te. 8 I... then (C) value. or the counting error
for. dltU8 I. greeter then thl dlt&8l. the vllue used In the c08pUtetion la one helf the "Inl- Detectable Activity (MDA).
IS-Io Standard .""en no leckground Tolerence Intervel vllue ueed I, the "In'- Detectable Activity (MDA)
"'n'_. HI. 1_. end Average beled on all Iv.llebe dltl.
Uell./Statlone In this group: SU06J
~
-------
Analyte
leekground AlAI
Velue. V.lue
Grosl Alphe
Groll lete
StrontlU8 89, 90
PlutonlU8 239, 240
AMrlclU8 241
'rltlU8
'otel UranlU8
7. 7450
9.8880
2.0400
0.0180
0.0420
257.18
1.8000.
, 7.0
5.0
; 8.0
.05
.05
500
5.0
- .
,
11
STATIO. ,.
TOTAL RADIOCBBHI8TRY COHCIHTRATIOH8
POR SURWAC8 WATIR
ALL COHCBHTRATIOH8 IH pCI/l
Il8Iber of
lelulu
lulber of .e.ult.
Above AlAI
....1-
V.lue
"Inl- .
Velue
..Aver... of
All V.l,,"
2 2 K.! 17 +
2 2 2l..! 17 +
2 0 1.5 < 1.00
J 0 .&lli...! < 0.01
2 0 .01 < 0.01
3 0 110 <400.00
3 2 13.S90 + 3.600
--lj +
-----D +
1.0
0.0050
0.0050
200
--U+
(+) Velue elCceed8 ARAI; (-) V.lue ellceed8 'eckground
,he ever... I. COIipIted bv flrat dete,..ln'.. the .r'th8Uc .en concentretlon et Indlvl_1 ..U.,.teU- end then Ullng thtl date to
cOllpUte the erlt"-tlc -en for the weU,'stetiona In thl. gr~. If e dIIt&8 Indicate. e I". then (C) vel... or the COUtU.. error
for e dIIt&8 I. greeter then the detU8, the velue used In the COIipItetlon II one helf the "Inl- Detectable Act'vlty (MDA).
IS-No Standerd .When no leckground Tolerenee Intervel velue used II the "Inl- Detectable Activity (MDA)
MiniMUM, "elCi~, and Averege based on ell eveil8be dete.
-------
"'\
8'1'ATIOII 103
TOTAL RADIOCHBMI8TRY CONCBIITRATION8
POR 8URPAC8 WATBR
ALL CONC811TRATION8 IN pCi/l
An8lyte
I.ckground ARAR
V.lue- v.tue
llulber of
.nul ta
Il8Iber of leaul t.
Above AlAR
.....-
Value
"tnl-
V.lue
. -Aver. of
All v.lue.
Gross Alpha
Groll leta
Strontlue 89. 90
Plutonlue 2)9. 240
Amerlctue 241
'rlth..
'ot.1 Urenhn
, ) ~ 2.00 --B+
7.7450 7.0 4 <
9.8880 .5.0 4 ) ~ < 4.00 -D+
2.0400 '8.0 4 0 H..! < 1.00 0.50
0.0180 .05 5 4 Li..! 0.01 --2:!1 +
0.0420 .05 4 ) ~ < 0.01 --L1! +
257.18 500 5 0 ~ <400.00 244
1.8000- 5.0 5 2 0.1oo --L!
(+) Value exceeds ARAR; ( ) Value exceeds 'ackground
'h. averege I. cClllpUted by flnt dlt.,..lnlng the arlth8t1c .an concentration at Indlvl"'l ","./atatl- and than uetne tht. dlt. to
cClllpUte the arlt'-tlc .an for the ...II./.tltlona In thl. grcqt. If a dlt'-8 Indlcat.. a I... than (c) velUl, or the cOW'Itlng error
for. datlll t. Ireater than the dlt... the value used In tha CClllpUutlon t. one half the "Inl- D.tectabl. Activity (fI»A).
IS-1o Standard -When no Background Tolerance Intervil value ueed I. the "IntiU8 Detectabl. Activity (fI»A)
"Inl_. "1IIi_. .nd "verage baaed on III avai I- dat..
Wella/Stltlons In this Iroup: SWI0)
~
-------
-------
.
.
SU~.ACE WATER ''''"TEr:t11l! ~EIo4EOIA.. ACilON PLAN
~>('V =I.A~S PLAN'", GOL!)EN, ::O..O"AOC
~&S ~,r~ waJ"'U'! .&Dc.na.~.
APPENDIX D
MILESTONE SCHEDULE
SURFACE WATER IM/IRAP/EA
, SOUTH WALNUT CREEK BASIN
OPERABLE UNIT NO.2
-------
TABLE D-1
MILESTONE SCHEDULE
,
SURFACE WATER IM/IRAP/EA
SOUTH WALNUT CREEK BASIN
OPERABLE UNIT NO.2
....
SOUTH WALNUT CREEK BASIN INTERIM MEASURE/INTERIM REMEDIAL ACTION PLAN/
ENVIRONMENTAL ASSESSMENT (IM/IRAP /EA) AND DECISION DOCUMENT
Submit Draft Proposed 1M/IRA Decision Document
June 19. 1990
Submit Proposed 1M/IRA Decision Document to EPA/CDH
September 18. 1990
Public Review of Proposed 1M/IRA Decision Document
September 26. 1990
Submit Draft Responsiveness Summary and Final
1M/IRA Decision Document
January' '. '991
Field Treatability Test System Installation Complete
April 12. 1991
Begin Field Treatability Testing
April 15. 1991
Complete 1M/IRA Construction
September 30. 1991
Begin Field Treatability Testing (Entire System)
October 30. 1991
Submit Draft Treatability Test Report
April 1. 1 992
Submit Final Treatability Test Program Report
June 2. 1992
SU~~ACE WATER 'NT'ERIIII I'\EIIIEOI.IU. A;:'nON PlAN
=lOCI(\' =..,A'rS P1..,ANT. GOLDEN. COLORADO
eog&; ~,r8'"NaIf"t..r.' ~a:'!b.~.~.m8!
-------
-------
,
.
SU~~4CE W4TE" I"''TERI'" ~"'EOIAJ.. 4CT1ON PLAN
~o('V =:"'<"'S :>:...4"11". GOLDeN. CO.ORACO
e;&g -.,rap wa..""",\, ~d.og'
APPENDIX E
ARAR TABLES FOR
SURFACE WATER CONTAMINANTS
-------
""'
TABLE E-1.1
CHEMICAL SPECIFIC ARARs
F(It VOlATILE (ltGAIIIC aJIIPCI8)S
I. SUlFACE ~TE. AT OPERABLE "IT MO. 2, SOUTH IMlIIIT CREEl(
Haxinun Con-
centration
In ARAR TBC ARAR Hazard CUJt iff1t/
Chemicat Surface Water' (ug/t) (ug/t) Reference Conment Cancer Rlsk*
(UII/ t)
Organic Compounds
Vinyt Chtorlde 15 2 wacc Surface Water; No orat RfD/
1.3E-04
Drinking Water Standard
Methytene Chtoride 44 5U No Standard RCRA Subpart F background 2.4E-03/1.1E-06
Is TBC
Acetone 130 100 No Standard Acetone is RCRA (40 CFR 2.8E-03/not
Part 264. Subpart F) considered an
Appendix IX constituent. orat carcimgen.
Background is TBC.
Carbon Tetrachtoride 605 5 wacc Surface Water; 2.0E-01/1.9£-05
Drinking Water Standard
1.1 Dichtoroethane 6 5U No Standard RCRA Subpart F background 1.4E-03/1.3E-05
is TBC
1.2 Dichtoroethene 56 5U No Standard RCRA Subpart F background 7. 1E-03 (based
is TBC CI'\ tnrslsaner)/
not consid-
ered an orat
carcinogen
1.1 Dichtoroethene 143 7 wacc Surface Water; 2.~-1IZ/1.2E-~
Drinking Water Standard
Tetrachtoroethene 280 LOU wacc Surface Water; Standard (0.8) is below 2.8E-03/1.5E-06
Fish and Water detection timit. therefore.
Ingestion Standard detection timlt is
ARAR-
Trichloroethene 260 5 wacc Surface Water; No orat RfD/
Drinking Water Standard 1.6E'06
Chloroform 82 1U wacc Surface Water; Standard is betow detection 2. 9E - 3/1. 7E - 7
Fish and Water limit. therefore, detection
Ingestion Standard I imit is ARAR
ru&qh... ....,.............\110' ~ 1 I
..
-------
.
.
TABLE E-1.2
CHEMICAL SPECIFIC AlAI.
FOR .TALS DETECTED ABOVE IAClCGIICUI)
II SUlFACE IMTEI AT OPERABLE "IT 10. 2, SOIJH IMLIIIT CREEK
Mall 1- Con-
centratlon
In ARAR TBC ARAR Hazard Quotient/
Chemical Surface Vater' (lII8/l) (Ing/l) Reference Conment Cancer Risk.
(1118/0
Metals
Al""lrun 25.4 0.2\1 wacc Surface Vater Aquatic Standard (0.150)ls below No oral RfD/not arsldered
Life Standard, Oefault to detection limit, an oral carcinogen
detection lI.lt. therefore, detection
limit Is ARAR.
Antimony 0.102 0.064 No Standard RCRA Subpart F 1.71E-03/notconsldered
background Is TBC. an oral carcinogen
Arsenic 0.01U 0.05(0.025U) wacc Surface Vater; Drinking The detection limit Is 0.7I1.25E-03
Vater Standard. selected as a remediation
goal because of the relative
high hazard quotient and
cancer risk associated with
the standard (0.05).
Barlun 2.02 1.0 wacc Surface Vater; Drinking 5.7E-01/not considered an
Vater Standard. oral carcinogen
Beryll I un 0.05n 0.1 wacc Surface Vater; O. 56/1.2E.02
Agricultural Standard.
Cadmium 0.0142 <0.005 waCt Surface Vater Aquatic Standard «0.005) Is 2.8E-01/notconsldered
Life Standard. detection lIlIit, an oral carcinogen
therefore, detection
limit is ARAR.
Calcium 152 No Standsrd No oral RID/not arsidered
an oral carcinogen
Chromium I" 0.212 0.01 waet Surface Vater; Analytical result is 2.8E-04/notconsidered
Aquatic Life Standard. total chromium. an oral carcinogen
Chromiun V 0.212 0.01 waec Surface Vater; Analytical result is 5.8E-02/notconsidered
Aquatic Life Standard. total chromium. an oral carcinogen.
-------
-._,
TAIlE E-'.2 (cant.)
. CIIBIICAL SPECIfiC -.
fOR .TALI DETECTED A80IIE IAaCGIOI8
.1 _fACE ..TEl AT Cl'£IA8I.E "IT 80. 2. SlllTI IMLIIIT ClEEK
"..1_. Can-
cent ratl an
In ARAR TBC ARAR Hazard Quotient/
Chemical Surface Water' (1118/1) (1118/1) Reference Conment Cancer Risk.
(",,/0
Metals (cant.)
Cobalt 0.132 0.05 wacc Ground Water 110 oral R~ anldered
Agricultural Standard Is TBC. en orel carcinogen
Copper 0.293 0.025U wacc Surface Water; Standard «0.025) is less 1.9E-02/notconsidered
Aquatic life Standard. than detectlan limit is an oral carcinogen
therefore, detection limit ARAR
is ARAR
Iron 204 (3.69) 1.0 (0.3) wacc Surface Water Analytical results are No oral RfD/nDt anldered
Standard total Iron; dissolved an oral carcinogen
Iran in parentheses
leed 0.215 O. 005U wacc Surfece Water; Standard «0.005) is less 110 oral RfDlnot anidered
Aquatic life Standard than detectian 11.lt, an oral carcinogen
therefore, detection ll.it
Is ARAR
lithl"" 2.56 2.5 wacc Ground Water No oral RfD/nDt anldered
Agricultural Standard an oral carcinogen
is TBC.
Magnesi"" 36.70 No Standard No oral RfD/rOt anldered
an oral carcinogen
Manganese 3.68 (0.643) 1.0 (0.05) wacc Surface Water Standard Analytical results are 1.4E-01 (7.1E-03)/not
total manganese; dis- considered an oral
solved IIInga08se In carcinogen
parentheses
Mercury 0.0024 0.0002U wacc Surface Water; Standard (0.00001)is less 1.9E-02/notconsidered
Aquatic life Standard. than detection limit is an oral carcinogen
therefore, detection ARAR
I imi t is ARAR
ev-8".-" .p,..I"",. \lCt-..-,
.
-------
.
.
TABlE E-1.2 (cant.)
CIIBIICAL SPECIfiC AlAlIa
Fell IlETALS DETECTED A8M IAaCGICIJI)
II SUlFACE "'TEl AT OPEIABLE "IT 10. 2. sonl IMI..IIIJ CREEK
"'111- Con-
centratlon
In ARAR TBC ARAR Hazard Quotient/
Chemical Surface Water" (ms/l) (ms/l) Reference C-.,t Cancer Risk.
(1liii/I)
Metals (cont.)
Mol vbdenuI 0.174 No Standard No oral RfD/mt anldered
an oral carcinogen
Nickel 0.246 O.04U wacc Surface Water: Standard «0.04) Is 5.8E-02/notconsldered
Aquatic Life Standard below detection lillit, an oral carcinogen
therefore, detection
liMit 18 ARM
Potasalun 21.5 No Standard No oral RfD/mt anidered
an oral carcinogen
Selenhn 0.016 0.01 wacc Surface Water: 9.5E-02/notconsldered
Drlnklna Water an oral carcinogen
Standard.
Sodiun 58.20 No Standard No oral RIO/rot anidered
an oral carcinogen
Stroot I"" 1.36 No Standard No oral RfD/mt anidered
an oral carcinogen
Vanadlun 0.555 0.1 wacc Groundwater: 4.08E-01/not considered
Agriculture Standard is TBC. an oral carcinogen
Zinc' 2.66 0.05 wacc Surface Water; 7.0E-03/notcoosldered
Aquatic Life Standard an oral carcinogen
-------
'.,.
TAIlE E-1.]
ClientAl. SPfClflC AlAI.
flit OTIIEI I_GAlliC allSJlUITS DETECTED MOllE IAClCGIIOIII)
II _FAtE "TEa AT OPEIIAII..E IIIIT 10. Z. SllUTI IMLIII1' CllEEIC
"all llIUII Con-
cent rat Ion
In ARAR TBC MAR Hazard Quotient/
Chemi cal Surface Water" <1118/ t) 118/ t) Reference Conment Cancer Rlsk*
<1118/1)
Conventional Pollutants
Nitrite 5.6 1.0 WQCC Surface Water Standard Analytical results are 2.9E-01/not considered
total nitrate plus nitrate an oral carcinogen
nitrogen. Reanalysis re-
qui red to detenllne if
nitrite ARAR Is ellceeded.
Nitrate 5.6 10.0 WQCC Surface Water Standard Analytical results are No oral RfO/not considered
total nitrate plus nitrite an oral carcinogen
ni trogen.
Chloride 170 250 WQCC Surface Water Standard No oral RfO/not considered
an oral carcinogen
Sulfate 74 250 WQCC Surface Water Standard No oral RfO/not cons idered
an oral carcinogen
Bicarbonate No oral R fO/not cons idered
a5 CaCO, 51,0 No Standard an oral carcinogen
T.O.S. ]300 400 WQCC Ground Water Standard No oral RfD/not considered
is TBC an oral carcinogen
~\.. ".,.\..Inul\lb -1.1.
.
-------
.
..
TABlE E-1.4
CIIOIICAl SPECIfiC MAlIa
f.. RADIOWClIDES DETECTED ABOVE BAClCGIICIII»
II SlltfACE ~TU AT OP£IAIlE "IT 10. 2, SWlH YlU.IIIT CREEl(
Maxinun Con-
cent rat Ion
In ARAR TBC ARAR HlZard Quotient/
Chemical Surface Water" (pCl/l) (pCl/l) Reference Conment Cancer Risk"
(pCl/l)
Radionucl ides
Gross Alpha 780 11 WQCC Surface Water Standard No oral RfD/NA
Gross Beta 570 19 WQCC Surface Water Standard No oral RfD/NA
PU238.231.2.o 3.3 0.05 WQCC Surface Water Standard No oral RfD/7.0 x 10.7,
8.0 X 10.8, 8.0 X 10.8
Am'" 1.3 0.05 WQCC Surface Water Standard No oral RfD/8.0 x 10.7
H3 0.00 500 WQCC Surface Water Standard No oral RfD/1.4 x 10.8
Sr"'''' 0.3 8 WQCC Surface Water Standard No oral RfD/1.2 x 10'8,
1.4 x 10'.
uraniun'''. 16.6 10 WQCC Surface Water Standard No oral RfD/3.3 x 10'.
(a)
(b)
U
J
B
ARAR
TBC
(c)
.
..
Maximum compound concentrations determined from all available data (see Appendix B).
Total concentration unless specified.
Detection limit
Estimated below detection limit
C~ also present in blank
Applicable or Relevant and Appropriate Requirement
To 8e Considered
Below mininun detectable activity (MDA)
Hazard quotient is ratio of daily intake at level of ARAR based on the consumption ot 2 liters/day and a body weight of 70 kg to the chronic
oral RfD (EPA, 1990b - Health Effects Assessment Summery Tables, Fourth Quarter, FY 1990). RfD = Agency-wide reference dose, developed by an
inter-office work group chaired by the Office ot Research and Development, u.S. EPA, Washington, D.C. Cancer Risk = ARAR (ug/l) x Carcinogenic
Slope Factor (ug/I r'
For radionuclides cancer risk = ARAR (pCi/l) x Pathway-specific unit risk (pCi/l)". The cancer risk is not applicable to gross alpha and
beta. Cancer risk depends not only on the form of radiation, but also on the radlonuclide etnitting the radiation because radionuclldes
selectively affect various organs.
-------
., .,
..,
TABLE E-2.1
AllAUSIS Of CIlEJlICAL SPECIFIC ARMs F«II VOlATILE
«llGAI8IC ID8'OIJI)S II -FACE ""Tel AT OPEIABlE "IT 10. 2, SWTH ""LIIIT ClEEK
.
RCRA WCC GrOtnt SOWA MaJllnun For Use In CVA Anblent Water Qual!ty WCC Surface
S\J)part F Water Quality Contemlnant Special Criteria for Protection of Water Qua tI ty
Concentration Standerdsb Level (MCL)C CirctnStances Aauat Ic li fe' Standards- ARAR
Chemical Limi t- (ug/t) (ug/t) (ug/t) SOWA'MCLGd Freshwater Acute/Chronlc (ug/t) (ug/U Comment
(ug/t) (ug/t)
Organic Compounds
Carbon Tetrachloride 5U 5 5 0 35,0001 5 5 WCC Surface Water
Quality Standard Is
applicable. RCRA
S\J)part F Is TBC.
1,2 Dichloroethene 5U 11,000'1 No Standard. RCRA
S\J)part F Is TBC.
1,1 Dichloroethane 5U No Standard. RCRA
S\J)part F is TBC.
1,1 Dichloroethene 5U 7 7 7 11,OOD'1 7 7 WCC Surface Water
Qual I ty Standard 18
applicable. RCRA
S\J)part F 18 TBC.
Tetrachloroethene 5U 0 5,200/840' 0.8 1.00 WCC Surface Water;
Fish and Water
Ingestion Standard
(0.8 ug/t) is BDL,
so detect Ion I I lilt
18 applicable
Acetone 10tf' No Standard. RCRA
S\J)part F Is TBC.
Methylene Chloride 5U No Standard. RCRA
S\J)part F 18 TBC.
~AG\.w h8p\","n'J1\lb .,.,
.
-------
.
.
TABLE E-2.1 (cont.)
ANALYSIS Of C~ICAl SPECIFIC AlAI. FOR VOlATILE
ORGAIIIC IDIPCUIDS II ~FACE IMTEI AT G'EIABLE IIIIT 10. 2. SOUTH UUIUT ClEEK
(a)
40 CFR Part 264.92 Subpart F releases from Individual hazardous substance
sites. (40 CFR 261. Appendix VIII, List of Hazardous Constituents)
5 eCR 1002-8, Section 3.11.5, Basic Standards for Ground Water
September 20, 1990.
40 CFR Part 141.61 National Prlmery Drinking Water Standards.
40 CFR Part 141.50 National Prlmery Drinking Water Stendards.
5 CCR 1002-8, Section 3.8.29, Final Rule Effective March 30, 1990.
Lowest observed effect level.
40 CFR Part 268.41 Subpart D . Treatment Standards.
RCRA 40 CFR 264, Appendix IX Ground Water Monitoring List Substance Not
Included In 40 CFR 261, Appendix VIII, List of Hazardous Constituents
Clean Water Act, Section 304 .
eo&a,...af8p\wIlnu1\lb 8"} .
ARAR -
BOL
LOR
MCL
MCLG -
RCRA -
SOWA .
TBC
U
WCC -
45,000/21,000'
5
5
WCC Surface Water
Cluellty Standard 15
applicable
WCC Surface Water
Quail ty Standard Is
applicable.
RCRA wacc Ground SOWA Maxlnun For Use In CWA Ant>ient Water Quat'lty waec Surface
Subpart F Water Quail ty Cont 81111 nant Spec! al Criteria for Protection of Water Quail ty
Concentrat Ion Standerdsb Level (MCL). CI rclftStences Aquat I c LI fe" Standards. ARAR
Chemical Uml t. (ug/t) (ug/t) (ug/t) SOWA/MCLGd Freshwater Acute/Chronic (ug/t) (ug/t) COIIIIIent
(ug/t) (ug/t)
Organic Compounds (cont.)
T r I chi oroethene 5U 5 5 0
Vinyl Chloride 1U 2 2 0
(b)
(c)
(d)
(e)
(I)
(g)
(h)
(k)
2
2
Applicable or relevant and approprlete requirements
Below detection limits
Lend disposal restrictions
Maxinun contaminant level
Maxlnun contaminant level goal
Resource Conservation and Recovery Act
Safe Drinking Water Act
To be considered
Detection Limit
-------
',",
TABLE E-2.2
ANALYSIS Of CHEMICAL SPECIFIC AltARs fill fl:TALS
DETECTED ABOVE BACl:GII(UI) II SUlfACE WATER AT OPERABLE ~IT 810. 2. SWTH WAL"T CREEK
RCRA WCC Ground SOIlA Ma)(l- for Use In CIIA Anblent Water Quat! ty WCC Surface
Subpart f Water Standard Contaminant Speclat Criteria for Protection of Water Quat I ty
Concentrat Ion H~ Heatth/ Levet (MCL)C ClrclRStances Aauatlc Life" Standard"
Chemicat L Imi t8 (mg/t) Agrlcut tureb (mg/t) SOIlA/MCLG freshwater Acute/Chronic Drinking Water/ ARAR
(mg/t) (mg/t) (mg/t) Agrlcutture (mg/t) Conment
(mg/t)
Metals
Allm!inun /5.0 0.150 0.2U wacc Surface Water
Aquatic Life Standard 1&
appt icaMe. Defautt to
detection tlmlt.
Antimony 0.06U No Standard. RCRA
Subpart F background
(0.064) 18 TBC.
Arsenic 0.05 0.05/0.1 0.05 0.8'/0.048' 0.05 0.05 waee Surface Vater
Drinking Water Standard
18 apptlcabte.
Barilm! 1.0 1.0/ 1.0 1.5' 1.0 wace Surface Vater
Drinking Vater Standard
18 apptlcabte.
Beryl I ilm! 0.005U /0.1 0.1'/.0053' 0.1 0.1 waee Surface Vater
Agrlcutturat Standard 18
apptlcabte.
Calinilm! 0.01 0.0110.01 0.01 0.005 0.003cf/0.0011h <0.005 0.005U waee Surface Water
Aquatic life Standard Is
apptlcabte. Defaul t to
detection tlmlt.
Calcilm! No Standard
Chromi 1m! III 0.05 (tot) 0.05/0.1 1.7"/0.2h 0.01 0.01 waee Surface lIater
Aquatic life Standard Is
appticabte.
8O.g\""f8P\-~ 2-2.
.
-------
.
.
'ABLE E-2.2 (cont.)
ANALYSIS Of CHEMICAL SPECIFIC AHARa FOR NE'ALS
DEJEC'ED ABOVE BAOCGRCUl) I. SUlFACE IMTER A' OPERABLE III" 110. 2. SOUJH IMLIUJ CIIEEI(
RCRA wacc GrOU'Wt SDIIA H811 i!IUII For Use In alA Anbient lIater Quelity wacc Surfece
Subpart F lIater Standard Contaminant Special Criteria for Protection of lIater Quell tv
Concentration H~n Health/ Level (HCL)o CircUllStances Aauatlc Life. Standard"
Chemical Limit" (mg/l) Agrlcul ture' (mg/l) SDIIA/HCLG Freshwater Acute/Chronic Drinking lIater/ ARAR
(1IIg/l) (mg/I) (mg/I) Agriculture (1IIg/1) Conment
(mg/l)
Metals (cont.)
Chromlun VI 0.05 (tot) 0.05/0.1 0.05 0.0012 0.016/.011 0.01 0.01 wacc Surface lIater
Aquatic Life Standard Is
applicable.
Cabal t 0.05 0.05 wacc Groundwater
Standard is TBC.
Copper 0.046 1.0/0.2 1.0 1.3' 0.018"/0.012" 0.025 0.025U wacc Surface lIater
Aquatic Life Standard is
applicable. Default to
detect Ion .111111 t.
Iron 0.3/5.0 0.3 1.0 (0.3) 1.0 (0.3) wacc Surface lIater
Drinking lIater Standard
Is applicable.
lead 0.05 0.05/0.1 0.05 0.002' 0.0082"/.0032 <0.005 0.005U wacc Surface lIater
Aquatic Life Standard Is
applicable. Oefaul t to
detection I II "it.
li thlun /2.5 waee GrOU'Wt lIater Agri-
cultural Standard is
TBe.
Magnes 1 un No Standard
Manganese 0.05/0.2 0.05 1.0(0.05) 1.0 waee Surface lIater
(0.05) Drinking lIater Standard
Is applicable.
-------
TABLE E-2.2 (cant.)
ANALYSIS Of CHEMICAL SPECIFIC ARAKs FOR METALS
DETECTED ABOVE BAD:GRCUI) II SURFACE YATER AT OPERABLE ~IT 10. 2. SOOTH YAl..T CREEl<
RCRA WCC Ground SOWA Mexlrrun For Use In CWA Ambient Water Quality WCC Surface
S~rt f Water Standard Cont l1li1 nant Special Criteria for Protection of Water Quall ty
Concentration H\88n Health/ level (MCL)o CI rCllllStances Aquatic life" Standard"
Chemical Limit" (mg/l) Agricultureb (RIg/I) SOWA/MClG freshwater Acute/Chronic Drinking Waterl ARAR
(RIg/I) (RIg/I) (RIg/I) Agriculture (mg/l) Comnent
(RIg/I)
Metals (cont.)
Mercury 0.002 0.002/0.01 0.002 0.003 0.0024/0.000012 0.0001 0.0002U WCC Surface Water
.1Aquatlc Life Standard
is applicable. Default
to detection limit.
Molybdenun /0.1 WCC Ground.water
Agriculture Standard Is
TBS.
Nickel 0.0185 /0.20 1.8'1.096' <0.04 O.04U \lQCC Surface Water
Aquatic life Standard Is
applicable. Default to
detection limit.
Potassil8l1 No Standard
Selenll8l1 0.01 0.01/0.02 0.01 0.045' 0.26/0.35 0.01 0.01 WCC Surface Water
Drinking Water Standard
is applicable.
Sodil8l1 No Standard
Strontll8l1
Vanadll8l1 1.65 /0.1 WCC Ground-water
Agricultural Standard Is
TBC.
linc 0.0511' 5.0/2.0 5.0 0.32'/0.047" 0.05 0.05 WCC Surface Water
Aquatic Life Standard Is
applicable.
"Notes on the next page.
eva".. h..wl8nut\8.:l ,
-0
-------
(a)
(b)
(c)
(d)
(0
(g)
(h)
(I()
(J)
ARAR
CIIA
MCL
MCLG
NS
R&A
RCRA
SDIIA
IIQCC
..."
c
40 CfR Part 264.92 Subpart f
5 CCR 1002-8, Section 3.11.5, Ground lIater Quality Standards
40 CfR Part 141.11 National Primary Drinking lIater Standards
5 CCR 1002-8, Section 3.8.29, final Rule Effective March 30, 1990 (Total Recoverable Concentrations). Most stringent standard from aquatic life, agricultural,
or drinking water is shown.
Proposed value as of October 1986
Lowest Observed Effect Level
Hardness dependent criteria (100 mull)
Clean Vater Act, Section 304
RCRA 40 CfR 264, Appendix IX, Ground Vater Monitoring List Substance not Included In 40 CFR 261, Appendix VIII, List of Hazardous Constituents
Applicable or relevant and appropriate
Clean Vater Act
Maximum Contaminant Level
Maximum contaminant Level Goal
No standard
Relevant and Appropriate
Resource Conservation and Recovery Act
Safe Drinking Vater Act
Colorado Vater Quality Control commission
-------
". .
TABLE E-2.3
MALYSIS OF CIIElnCAl SPECIFIC ARAlIa F. OTHER I-GAlliC
CDlSTITUEITS DETECTED ABOVE IlAClCGIICUII II SUlFACE IMTER AT OPERABLE &JIlT 10. 2, 5O,ITII IMLIIIT CREEl(
RCRA wace Ground $OWA Maxlnun For Use In CWA Anbient Water Qual ity wace Surface
S~rt F Water Standard eont8lllinent Special Criteria for Protection of Water Que I I ty
Concent rat Ion HLI1I8n Health/ Level (MCL)G eircl.IIIStances AQUatic Lifek limited ARAR
Chemical Limit' (1119/1) Agriculture' (1119/1) SDWAlMCLG. Freshwater Acute/Chronic S t anda ref" (unless
(mg/I) (mg/I) (mg/l) Drinking Water/ otherwise
Agriculture noted) eonment
(1119/1)
Conventional Pollutants
Nitri te 1.0 as ./ 1'/10h 1.0 waee Surface Water
10.0 as . Standard is
applicable
Nitrate 10.0 as N/ 10 1o'/10~ 10.0 waee Surface Water
100 a5 N02+N~-N Standard I s
applicable
Chloride 250/ 250 250/ 250 waee Surface Water
Standard Is
appl icable
sulfate 250/ 250' 250/ 250 waee Surface Water
Standard Is
applicable
Bicarbonate
as eacoJ No Standard
-oag\8w h8P\w8tnul\tb.2 3.
.~
-------
TABLE E-2.] (cont.)
ANALYSIS Of CIlElfICAL SPECIFIC AllARs Flit OTIlER I_GAlliC
aIISTITUEITS DETECTED A80IIE IlACl(GIKIJI) II SUlFACE IMTEI AT OPERABLE IIIIT 10. 2. SUIT" IMUI" ClEEK
.
c.
Chemical
RCRA
SlAJpert F
Concentration
Llml to (mg/ t )
wacc GrOtA'Xt
"ater Standard
Hl.8Mn Health/
Agrlcutture"
(mg/l)
SOWA "8111 nun
Contaminant
Levet (MCL)c
(mg/t)
For Use In
Spec I at
Clrc\.lllStances
SD"AI"CLG
(mg/t)
C"A Ambient Water Quality
Criteria for Protection of
AQUat I c LI fe"
Freshwater Acute/Chronic
(mg/t)
wacc Surface
"ater Quatlty
Limited
Standard"
Drinking "ater/
Agrlcutture
(mg/t)
ARAR
(untess
otherwise
noted)
Conment
T .0. S.
Conventional Pollutants (cont.)
500'
400 mg/l or
1.25 times
beckgrOtA'Xt,
whichever
is least
restrictive
(a)
(b)
(c)
(d)
(I)
(g)
(h)
(I)
(k)
40 CFR Part 264.92 Subpart F reteases from Indivlduat hazardous substance sites
5 CCR 1002-8, Section ].11.5, Groundwater Quality Standards
40 CFR Part 141.11(b,c) latlonat Primary Drinking "ater Standards
5 CCR 1002-8, Section ].8.29, Final Rule Effective March ]0; 1990.
40 CFR Part 14].] lationat Secondary Drinking "ater Standards
To be apptied at the point of water suppty Intake
In order to provide such a reasonabte margin of safety to attow for
unusual situations such as extremety high water Ingestion or nitrite
formation In sturrles, the 1°3-1 ptus 1°2-1 content in drinking waters
for tlvestock and pouttry shoutd be timlted to 100 ppm or tess, and the
N02-1 content alone be t Imlted to 10 ppm or tess.
A combined totat of Iltrlte and Iitrate at the point of intake to the
domestic water suppty shall not exceed 10 mg/l.
Clean "ater Act, Section ]04
8060uw h8P\W*",t\tb .2 3
ARAR
alA
"CLG
15
RCRA
SOYA
wacc
wacc Ground "ater
Standard Is TBC.
Apptlcabte or retevant and appropriate requirements
Ctean Water Act
"axl~ contaminant tevet goat
10 standard
Resource Conservation and Recovery Act
Safe Drinking Water Act
-------
..0,
TABLE E-2.4
AllALtSIS Of CHElUCAL SPECIFIC AIAIs F. IlADloaJellDES
DETECTED AIDVE IAClUiltClJl) II _FACE IMfEl AT OPEIABLE IIIIT 10. 2. SOUTIIMLIIIT ClEEK
Chemical
RCRA WClCC GrOlnf SOVA "11I1nun For Use In CVA Amlent Vater Qualltv wacc Surface
SlJ)pert F Vater Quality Contemlnant Special Criteria for Protection of Vater Qual I ty
Concentration Stand8rdsb Level (MCL)c CirclJIIStances Aauetlc life- Standardsd ARAR
limit" (pCl/t) (pCl/t) (pCl/l) SDVA/MCLG Freshwater Acute/Chronic (pCl/l) (pCl/l) Conment
(pCl/l) (pCi/l)
Radionucl ides
Gross Alpha
15 15 11 11 wace Surface Vater
Standard for Valnut
Creek Is applicable
4 mrellV'yr" 50 19 19 waee Surface Vater
Standard for Valnut
Creek Is applicable
15 40' 0.05 0.05 wace Surface Vater
Stenderd 18
applicable
4' 0.05 0.05 waee Surf Ice Vater
Standard 18
applicable
20,000 20,000 500 500 WGCe Surface Vater
St8ndllrd la
eppll cable
8 8 8 8 wacc Surface Vater
Standard Is
Ippllcable
Gross Beta
PU1J..7J..140
Am1"
M.I
Sr...OO
80&0\.'" h8p\-"*,ul\lb ., .
.
-------
.
TAiLE E-2.4 (cont.)
AllALYSIS Of CHEMICAL SPECIFIC ARM8 FOt UDUIRJClIDES
DETECTED ABOVE IAClGIICUI) I. _FAa _TEl AT OPERABLE UlIT m. Z. SOUTH IMl;IIIT atEEIC
<-
Chemical
RCRA
Subpart F
Concent rat ion
limit" (pCi/t)
wacc Ground
Water Qual i ty
Stendardsb
(pCi/l)
SOWA Max inun
Cont8ll1inant
level (MCl)'
(pCi/l)
CWA Ant)ient Water Qual i ty
Criteria for Protection of
Aquatic Life'
Freshwater Acute/Chronic
(pCi/l)
wacc Surface
Water Quail ty
Standards'
(pCi/t)
ARAR
(pCi/t)
Comnent
For Use In
Special
C I rClJIIStences
SDWA/MClGd
(pCi/l)
UranilB"."
Radionuclides (cont.)
(8) -
(b) -
(c) -
(d) -
(e) -
(f) -
(k) -
40 CFR Part 264.92 Subpart F releases from Individual hazardous aubstance sites
5 CCR 1002-8, Section 3.11.5(B), Basic Standards Applicable to Ground Waters of the State
40 CFR Parts 141.15, 16, National Primary Drinking Water Standards
5 CCR 1002-8, Section 3.8.29, Final Rule Effective March 30, 1990.
For beta and photon emitters, If two or more radionuclldes are present, the SUII of their
annual dose equivalent to the total body or to any organ shall not exceed 4 IIIrem per year.
Except 10r Tritiun and Strontiun 90 the concentration 01 men-made radlonuclldes causing
4 mrem total body or organ dose equivalents shall be calculated on the basis 01 a 2 liter
per day drinking water Intake using the 168-hour data listed in "Maxlnun Permissible Body
Burden and MaKimun permissible Concentration of Radionuclides In Air or Water for
Occupational hposure," NBS Handbook 69, as 8II1ended, August 1963, US Department of
Coomerce.
Proposed value in drinking water yielding a risk equal to that from a dose rate 01 4
mrem/year, Septent)er 30, 1986 (51 FR 34859).
Clean Water Act, Section 304.
Am
ARAR -
CWA
H3
MCl
MClG -
pu
RCRA -
SDWA -
Sr
wacc -
.0"'0'1.... hlp\w'*'UI\tb..1 4
10
10
wacc Surface Water
Standard for Walnut
Creek is applicable
Amer I cI UII
Applicable or relevant and appropriate requirements
Clean Water Act
Tri t lUll
MuillUll cont8ll11nant level
MaKlnun cont8ll11nant level 90al
Plutonhlll
Re80urce Conservation end Recovery Act
Safe Drinking Water Act
Stront"...
-------
Act ion
Treatment
Hazardous
"aste
Generation
Hazardous
"aste
Transportation
Excavation/
consolidation
Ground-"ater
Diversion
.low-lnpl...""""'..,3-I.
Reaulrement
BOAT standards for spent
solvent wastes and dloxln-
containing wastes are based
on one of four technologies
or conDlnatlons; for waste
waters, (1) steM stripping,
(2) biological treatment, or
(3) carbon absorption [alone
or In conDination with (1)
or (2»); end for all other
wastes, Incineration. Any
technology may be used,
however, If It will achieve
the concentration levels
specified.
Standards applicable to
generators including waste
accumulatlon,recordkeeplng,
container labelling,
manifesting, etc.
Hazardous waste shipment
off-site Is subject to DOT
regulations, manifesting,
recordkeepi ng, and di scharge
cleanup, etc.
Consolidation In storage
pi les/storage tanks will
trigger storage require'
lllents.
Placement on or In land
outside unit boundary or
area of contamination will
trigger land disposal
requirements and
restrictions. (See Table E'
3.2 for allowable consti-
tuent concentrations.)
Excavation of soi I for
construction of slurry wall
may trigger cleanup or land
disposal restrictions.
-. ,
TABLE E-J.1
ANALYSIS OF ACTION SPECifiC ARAts
fill REMEDIAL ACTIONS AT OPERABLE ..n, 2, SOOT" IMLIIIT CREEK
prereaul site
effective Novenber 8, 1988,
disposal of contaminated soil
or debris resul t Ing frOll!
CERCLA response actions or
RCRA corrective actions Is
subject to land disposal
prohibitions and/or treatment
standards established for
spent solvent wastes, dloxln-
containing wastes, and
"California List" wastes.
"aste must be Identifiable as
hazardous per 40 CFR Part 261
"astes nust be Identifiable as
hazardous per 40 CfR Part 261.
Movement of hazardous waste
(listed or characteristic)
from one unit or area of
contamination Into another.
Consolidation within a unit or
area of contamination does not
trigger applicability.
RCRA hazardous waste placed at
site after November 19, 1980,
or movement hazardous w8ste
f rom one uni t, area of
contamination, or location
Into another unit or area of
contamination.
Citation
RCRA Sections
3004(d)(3), (e)(3)
42 U.S.C.
6924(d)(3), (e)(3)
40 CFR Part 262
40 CFR Part 263
40 CFR Part 264
Subpart L/ 40 CFR
Part 264 Subpart J
40 CFR 268
(Subpart D)
See EXC8vat lon/
Consolidation
~
. Applicable
Applicable
Applicable
Applicable
RIA
R&A
Conments
Movetnent of excavated soil on-site or
transportation of soil off-site for
disposal must be treated to attain
levels achievable by best demonstrat
ed avai lable treatment technologies
before being land'disposed.
"astes generated In proposed action.
-y be identifiable as hazardous
wastes. Examples...y Include
treatment sludge, excavated soi ls,
used treatment ...terlals. RIA If
wastes are not hazardous.
"astes Identifiable as hazardous must
comply with applicable hazardous
waste requirements for off-site
shipment. RIA if not hazardous.
RCRA requirements for storage In
waste piles or tanks are applicable
to Interl~ storage of excavated soil
destined for consol idatlon or off-
site disposal.
Soil excavated during installation Is
subject to land disposal restrictions
for wastes If placement occurs
outside the area of contamination.
Requirements are applicable for RCRA
hazardous waste; R&A If not RCRA
hazardous waste.
See Excavation/Consolidation
.
-------
Action
Treatment or
Storage in
Tanks
..a,""'.ltopl_"""bl.C).I.
Reaulrement
hnks IIIJSt have sufflctent
sheii strength (thickness),
and, for ciosed tanks,
pressure controis, to assure
that they do not coUapse or
rupture.
Yaste must not be
IncOlTplltlbie with the tank
materlai unless the tank is
protected by a liner or by
other !lleans.
New tanks or c~ts III.Ist
be provided with secondary
contalnnent.
Tanks MUSt be provided with
controis to prevent
overfliilng, and sufficient
freeboard IIIIIlntalned In open
tanks to prevent overtoppi ng
by wave act ion or
prectpl tat Ion.
Inspect the foliowlng:
overflliingcontrol, control
equipment, monitoring data,
waste level (for uncovered
tanks), tank condition,
above-ground portions of
tanks, (to assess their
structural Integrity) and
the area surrounding the
tank (to Identify signs of
leakage).
Repair any corrosion, crack,
or leak.
At closure, remove all
hazardous waste and
hazardous waste residues
from tanks, discharge
control equipment and
discharge confinement
structures.
TABLE E-3.1 (continued)
/\MAlTSIS OF ACTION SPECIFIC AlARs
fell REMEDIAL ACTIONS AT OPERABLE "IT 2, SIOUTH WAUl.. tREEI
Prereaulslte
RCRA hazardous waste (lIsted
or characteristic), held for
temporary period before
treatMent, disposal, or
storage elsewhere, (40 CFR
264.10) In 8 tank.
Citation
40 CFR 264.190
40 CFR 264.191
40 cn 264.193
40 CFR 264.194
40 CFR 264.195
40 CFR 264.196
40 CFR 264.197
.
4..
~
Conments
RIA
Applicable to treatment and storage
tanks used In treating or containing
water contaminated with hazardous
waste. RIA If units would be
excluded under RCRA, such as
wastewater treatment units or If
wastes are not RCRA hazardous waste.
RIA
RIA
RIA
RIA
RIA
-------
~
Treatment or
Storage In
Tanks (cont.)
Container
Storage
(On-Site)
.'-'-iropl_bu"bI-d-l.
Reaul rement
Store Ignl table and react Ive
waste so as to prevent the
waste from Igniting or
reacting. Ignltabte or
reactive wastes In covered
tanks must coqlly with
buffer zone requirements In
IlFl8111118bte and CodJustlbte
Liquids Code," Tabtes 2-1
through 2-6 (Natlonat Fire
Protection Association, 1976
or 1981).
Containers of
waste must be:
hazardous
. Maintained
condition;
In
good
. COII'pBtlble with hazardous
waste to be stored; and
. ctosed during storage
(except to add or remove
waste).
Inspect container storage
areas weekly for
deterioration.
Place containers on a
sloped, crack-free base, and
protect from contact wi th
accllTUlated t lquid. Provide
containment system with a
capacity of 10% of the
volune of containers of free
liquids. Remove spitted or
leaked waste In a timely
manner to prevent overff ow
of the containment system.
Keep containers of Ignitable
or reactive waste at least
50 feet from the facility's
property line.
TABLE E-].1 (continued)
ANALYSIS OF ACTIOI SPECifiC AlAR.
fClt REMEDIAL ACTiOIS AT OPERABLE ~IT 2. SiDUTH IMllUT CREEK
Prereaulslte
RCRA hazardous waste (listed
or characteristic) held for a
temporary period before
treatMent. disposal. or
storage elsewhere. In a
container (I.e.. any porteble
device In which a materlet Is
stored. transported. disposed
of. or handled) (1,0 CFR
264.10).
Citation
~
.R&A
40 CfR 264.198
40 CFR 264.171
Appl leabl e
40 CfR 264.1n
40 CFR 264.173
40 CFR 264.174
40 CFR 264.175
40 CfR 264.176
Conments
RCRA container storege requirements
are applli:ebte If hezsrdous .,utes
are stored, R&A If stored .,astes ere
not RCRA hezardous wastes.
.
-------
Action
Container
Storage
(On-Site)
(cont)
Off-Site
Treatment
Storage or
Disposal
e.-'.'-w.i,."..,.ba;i\lbl-cJ.I.
ReQUirement
Keep IncOll'p8tible materials
separate. Separate
incompatible materials
stored near each other by a
dike or other barrier.
At closure, remove all
hazardous waste end residues
from the contalnnent system,
and decontaminate or remove
all containers, liners.
In the case of any removal
or remedial action Involving
the transfer of any
hazardous slJ)stance or
pollutant or cont_Insnt
off - s Ite, such hazardous
slJ)stance or pollutant or
contaminant shall only be
transferred to a facility
which' is operating In
compl iance wi th sect,lon 3004
and 3005 of the Solid Vaste
Disposal Act (or where
applicable, In compliance
with the TOil Ie SIJ)s t ances
Control Act or other
applicable Federal law) and
all applicable State
requirements. Such
slJ)stance or pollutant or
contaminant may be
transferred to a land
disposal facility only If
the President determines
that both of the following
requirements are met:
. The uni t to which the
hazardous substance or
pollutant or contaminant
is transferred Is not
releasing any hazardous
waste, or constituent
thereof, Into the ground
water or surface water or
soil.
. .
TABLE E-3.1 (continued)
ANALYSIS OF ACTION SPECIFIC ARARs
FOR REMEDIAL ACTIONS AT OPERABLE UlIT 2, SOUTH YALIlUT CREEK
PrereQUisite
Citation
40 CFR 264.177
40 CFR 264.178
SARA section
121 (d)(2)(C)
m!
Applicable
.
..
Comments
Applicable to the off'slte treatment,
storage, .or disposal of wastes
generated during on-site remedial
-------
Act ion
Off-Site
Treatment
Storage or
Disposal
(cant)
Discharge
of Storm
lIaters
Discharge
of lIater into
Surf ace lIater
Bodies
.~w.inp\..tmA\lbI ~ 1.1.
Requi rement
. All such releases from
other units at the
facility are being
controlled by a
corrective action program
approved by the
Administrator under
subtitle C of the Solid
Vaste Disposal Act.
Vastes IllUSt be treated using
technology or to concentra-
level by best demonstrated
available technology (BOAT)
for each hazardous
constituent in the ..aste,
prior to land disposal.
(See Table E-3.2)
Requires storm water
discharges to be perml tted
under the Federal (or state)
National PotlutlonDlscharge
elimination Systems (NPDES)
program. Different
requirements are applicable
for di fferent classes and
types of discharges.
An NPOES perlllit Is required
for discharging water into
surface water bodies.
All surface water discharges
nust be In coq>lIance with
recently promulgated
Colorado Stream Discharge
Standards
".-\
TABLE E-3.1 (continued)
ANALYSIS OF ACTION SPECIFIC ARARs
FOR REMEDIAL ACTIONS AT OP£RABlE UNIT 2, SOOTH WALNUT CREEK
Prerequisite
Wastes must be identifiable as
hazardous per 40 CFR Part 261
Citation
40 CFR Part 268
40 CFR 122.21(g)
40 CFR 122.26, and
40 CfR 122.28
40 CFR 122 and
40 CfR 125
5 CCR 1002.8
ARAR
Applicable
RIA
RIA
RIA
Conments
Applicable to wastes, other than
treated effluent, such as treatment
sludge, excavated salls, used
treatment In8terials. Also appl icable
to on-site land disposal or
"placement" outside the area of
contamination. RIA if not RCRA
hazardous waste.
Treated effluent ..Ill be
and treated in Pond 8-5,
subject to NPOES permi t,
discharge off-site.
Treated effluent will be
end treated in Pond 8-5,
subject to NPOES permit,
discharge off-site.
Treated effluent will be
and treated in Pond 8-5,
subject to NPOES permi t,
discharge off-site.
.
<
collected
which is
prior to
collected
which Is
prior to
collected
which is
-------
Action
Effluent
Guidel ines
and Standards:
Pre-Treatment
Standards
Discharge of
Treatment
System
Effluent
U.S. EPA
Ground-Water
Protection
Strategy
National
AlT'bient Air
Quality
e.a.~_.i,.,,\...1n.t\d"-e).I.
R!!QUi rement
This section establishes
pre-treatment standards
(both general and
categorical) for the control
of poltutant discharges into
Public OWned Treatment Works
(POTW). Discharge of POT"
nust not cause pass-through
interference, violation of
specific prohibitions, or
violations of local
I Imitations or ordinances.
POTW should el ther have an
EPA-approved pre-treatment
program or have sufficient
mechanl SIIIII to meet the
requirements of the national
pre. treatment program In
accepting CERClA waste.
Use of best available
technology (BAT)
economlcalt y achievable Is
required to control toxic
and non-conventional
pollutants. Use of best
conventional pollutant
control technology (BCT) is
required to control
conventional pollutants.
Technology-basedllmltatlons
may be detenlllned on a case-
by-case basis.
The strategy Includes
guidelines on classifying
ground water for EPA
decisions affecting ground
water protection and cor-
rective actions. Criteria
include ecological I~rt-
ance, replaceablilty, and
vulnerabl I I tyconsiderat Ion.
National alT'blent air qual Ity
standards have been set to
attain and maintain primary
and secondary standards to
protect publ ic heal th and
the env Ironment. Requi re-
ments Include a major-source
permit, prevention of sig-
nificant deterioration
permit, non-attainable area
permit, and visibil ity
permi t.
TABLE E-3.' (continued)
ANALYSIS OF ACTION SPECIFIC ARAts
fmt REMEDIAL ACTU*S AT OPERABLE ~IT 2, SUUTH ~L"'T CREEK
Prer!!QUIs i te
The protection strategy does
not involve applicable ARARs
but does contain policy
statements to be considered.
Citation
1,0 CFR 1,03.5
40 CFR 122.44
CAA Section 109
and 40 crR 50
.
.....
ARAR
RIA
Comments
Treated effluent wltl be
and treated In Pond B-5,
subject to NPDES permit,
discharge off-site.
collected
which Is
prior to
RIA
The r8llledlal alternatives at Operable
Unit 2 ~y Include the dlacharge of
treatment systeM effluent.
TBC
This strategy Is to be considered
regarding ground water remedial
alternatives for Operable Unit 2.
RIA
Remedial actions at Operable Unit 2
that may result In new sources 01 air
emissions include Incineration,
excavation, and air stripping of
-------
Action
New Source
Performance
SUndards .
Trensportation
of Hazardous
Materials
Environnenul
Iq>act of
Federal
Actions
Yorker
Safety
Emergency
Plamlng,
Preparedness,
and Response
for Operations
...lrop\_bu\Obl.,}.I.
Requirement
Standards for new sources of
air emissions. Requirements
are source-specific.
Specific DOT requirements
exist for labeling,
packaging, shipping
papers/manifesting, Ind
transporting by ralt,
aircraft, vessel, Ind
highway.
A statement of envl rOf1llll!ntal
Impact Is required.
Establishes provlalons
applicable to and binding on
ail federal agencies for
Inplementlng the proceci.lral
requirements of the National
Environmental Poi Icy Act
(NEPA). Includes proceci.lres
for plamlng (Part 1501),
preparing environmental
Inpect statements (part
1502), decision-making (Part
1505), and conpllance (Part
1501) .
occupet ional Safety and
Heal th program for DOE
. contractor enployees at
government-owned
contractor-operated
facilities.
Provide coordination
direction of plennlng,
preparedness, and response
to operational emergencies
In which there is a
potential for personal
injury, destruction of
property, theft, or release
of toxic, radioactive, or
other hazardous material
wh i ch present a potent lal
threat to health, safety, or
the envi ronnent-
..,
TABLE E-3.1 (continued)
---lYSIS OF ACTI~ SPECIFIC ARAts
FOR REMEDIAL ACTI~S AT Il'ERABlE a.l1T 2. SOJTH IMURn CREEK
Prerequisite
Need to determt"ne I f these
standards apply to potential
remedial actions.
Citation
CM Sect i on III
49 CFR 100-199
NEPA Section
102(2)(c) and 40 CFR
1500-1508;
DOE 5440.1C
DOE 5483.1A
DOE 5500.2
a!M
R&A
Applicable
RIA
TBC
TBC
Comments
Applicable to wlstes or materials
Ihlpped off-site.
EPA, COH, and DOE have reached
agreement on the appttcabH ity of
NEPA to RCRA/CERClA actions.
.
-------
Action
Generat
Environmentat
Protection
Program
Environmentat
CoqIt i ance
Issue
coordination
Hazardous and
Radioactive
Milled Waste
Program
Radiation
Protection
Packaging and
Transportation
of Hazardous
Materials,
Hazardous Slb-
stances,
hazardous
wastes, and
radioactive
materials
CoqIrehenslve
Envlrorwnental
Response,
CoqIensatlon
and Liabit ity
Act Program
Envlronmentat
Protection
Safety, and
Heal th
Protection
Information
Reporting
Requirements
cc.alo...lnp\-trul&bI.d.l.
ReQUirement
Estabtishes envlronmentat
protection program
r e qui rem e n t s ,
aut h 0 r I tie s , and
responslblt Itles for DOE
operations for ensuring
cllq)t lance with federat and
stateenvlr~t protection
taws and. regutatlons,
federat ellecutlve orders,
and Internat department
potlcles.
Estabt I shes DOE requirements
for coordination of
significant envlr~tat
cllq)t lance Issues.
Estabtlshes DOE hazards and
radioactive milled waste
pot Ides and requirements
and IqJtements RCRA.
Estabtlshes radiation
protection standards and
requirements Including
occupatlonatly related
ellposure of Individuals In
controlted areas.
Establishes requirements for
packaging and
transportat Ion.
Establishes basic
requirements for
Implementation of the
Superfund at DOE fecit I ties.
Establishes requirements and
procedures for report Ing
Information having
envirorwnentat protection,
safety, or health
significance for DOE
operations.
TABLE E-3.1 (continued)
"-"LYSIS Of "CTIU. SPECIFIC ARARs
Felt REMEDIAL "CJlU.S AT OPERABLE UIIIT 2. SOOT" ""UIUT CREEK
Prerequisite
Citation
DOE 5400.1
DOE 5400.2"
DOE 5400.3
DOE 5480.1
OOE 5480.3
DOE 5480. 14
DOE 5484. 1
.
'-
~
TBC
Conments
TBC
TBC
TBC
TBC
TBC
-------
Action
Radioactive
Waste
Management
low.irop\_lnLclibl.d.l.
Requirement
Establishes pol icies and
guldelloes by which DOE
manages radioactive waste,
waste byproducts, and
radioactively contaminated
surplus facilities.
TABLE E-3.1 (continued)
AlALYSIS OF ACTION SPECIFIC ARAta
FOR REMEDIAL ACTIONS AT OPERABLE WIT 2. san" WALIIIT CREEK
Prerequisite
Citation
DOE 5820.2A
ARAR
Conments
TBC
.
-------
'-.I
..
Constituent
Aluminum
Antimony
Arsenic
Barium
Beryllium
Cadmium
Calcium
Cesium
Chromium (total)
Cobalt
Copper
Iron
Lead
Lithium
Magnesium
Manganese
Mercury
Molybdenum
Nickel
Potassium
Selenium
Sodium
Strontium
Vanadium
P lf38.238.240
Am2.'
H3
"9&9. _tr&C wain",.. t""'~2
TABLE E-3.2
ACTION-SPECIFIC ARARS FOR CONSTITUENTS
IN WASTES FOR OFF-SITE DISPOSAL OR
ON-SITE PLACEMENT, OPERABLE UNIT NO.2
SOUTH WALNUT CREEK INTERIM REMEDIAL ACTlON*
Potential
Waste Code
DOO4
0005
P015 (as product
dust)
DOO6
0007
0008
0009
U151
FOO6-FOO9
F011-F012
0010
Treatment
Standard (mall)**
Best Demonstrated Available
Technology (BOAT)
Basis for Standard
5.0 (in extract)
100
Vitrification
Metals Recovery'
1.0
Chemical Precipitation
5.0
Reduction and Stabilization
5.0
Stabilization
0.20
0.025
Acid Leaching and Chemical
Precipitation
0.32
Chemical Precipitation, Settling,
Filtration, and Stabilization
5.7
-------
TABLE E-3.2 (continued)
ACTION-SPECIFIC ARARS FOR CONSTITUENTS
IN WASTES FOR OFF-SITE DISPOSAL OR \
ON-SITE PLACEMENT, OPERABLE UNIT NO.2
SOUTH WALNUT CREEK INTERIM REMEDIAL ACTlON*
Best Demonstrated Available .
Potential Treatment Technology (BDAT)
Constituent Waste Code Standard (malt).. Basis for Standard
S,-,80
UraniumtolaJ
Carbon Tetrachloride U211 5.6 Incineration or Fuel Substitution
FOO1 0.96 Incineration
1,2 Dichloroethene U079 33 Incineration or Fuel Substitution
1,1 Dichloroethane U076 7.2 Incineration or Fuel Substitution
1,1 Dichloroethene U078 33 Incineration or Fuel Substitution
T etrachloroethene U210 5.6 Incineration or Fuel Substitution
FOO1 0.05 Incineration
Acetone UOO2 160 Incineration or Fuel Substitution
FOO3 0.59 Incineration
Methylene Chloride uoeo 33 Incineration or Fuel Substitution
FOO1 0.96 Incineration
FOO2 0.96 Incineration
Trichloroethene U228 5.6 Incineration or Fuel Substitution
FOO1 0.91 Incineration
FOO2 0.91 Incineration
Vinyl Chloride U043 33 Incineration or Fuel Substitution
Multi-Source Leachate2 F039
*
Land Disposal- Restrictions at 40 CFR Part 268
**
Treatment standards are presented for non-wastewaters
Standard is expressed as a specific technology
2
U.S. EPA added listed hazardous waste code F039 to 40 CFR 261.31 June 1, 1990 (55 FR 22520) and
defined it as .'eachate resulting from the treatment, storage, or disposal of wastes classified by more than
one waste code under [40 CFR Part 261] Subpart D, or from a mixture of wastes classified under Subparts C
and D of this part.. If this waste code is deemed applicable to a waste, the waste must meet the treatment
standards (see 40 CFR Part 268 Tables CCW and CCWE) prior to land disposal.
-------
LOCATION
Fault zones
Aood plain
Siting of Hazardous Waste
Disposal Sites
Siting of Wastewater
Treatment Facilities
Siting within an area where
action may cause Irreparable
harm, loss, or destruction of
significant artlcfes.
Siting on or near hIstoric
property owned or controlled
bV Federal agency.
89&0\ ....I,,,,,\_lnU\\lbI...4
. ,
TABLE E-4
ANAL VSIS OF LOCATION-SPECIFIC ARARa
FOR REMEDIAL ACTIONS AT OPERABLE UNIT NO.2, SOUTH WALNUT CREEK
CITATION
40 CFR 264.18(a)
40 CFR 264.18(b)
Colorado Hazardous Waste
Act, Sections 25-15-101,203,
208, 302
Colorado Water Quality
Control Act Section 25-8-202
and 25-8-702
36 CFR Part 65, National
Historic Preservation Act
36 CFR Part 800, National
Historic Preservation Act
REQUIREMENT
RCRA regulations specify that
hazardous waste treatment,
storage, or disposal must not
take place within 200 feet of a
Holocene fault.
Any RCRA treatment, storage,
or disposal facility which lies
within a 100-year floodplain
must be designed, constructed
and operated to avoid washout.
Outlines sitIng criteria for
hazardous waste disposal sites.
CDH Water Quality Control
DMslon must approve locations
of wastewater treatment
facilities.
Planned actions must avotd
threatening significant scientific,
prehlstorfcal, historical, or
archeological data.
Action to preserve historic
properties; planning of action to
minimize harm to Nallonal
Historic landmarks, Included In
or eligible for the National
Aeglster of Historic Places
.
ARAA
.D:fE*
A&A
R&A
R&A
R&A
Applicable
Applicable
.
t..
.cOMMENT~
No faults displaced during
Holocene limes exist within.
200 feet of this site.
This site Is not located within a
100-year floodplain.
Although the proposed action
Involves the treatment of water
rather than disposal of
hazardous wastes, these
crfterla are considered In the
sitIng of the unit.
Applicable to domestic
wastewater treatment facilities,
relevant and appropriate to the
proposed action.
Proposed actlvftles wKl not
threaten significant scientific,
historic, prehistoric, or
archeological artifacts.
Proposed actlvftles will not
disturb known or suspected
historic sites. Aefer to
-------
TABLE E-4 (continued)
ANALYSIS OF LOCATION-SPECIFIC ARARa
FOR REMEDIAL ACTIONS AT OPERABLE UNIT NO.2, SOUTH WALNUT CREEK
LOCATION
Siting on critical habitat of
endangered or threatened
species.
CITATION
50 CFR Paris 200. 402.
33 CFR Paris 320-330
REQUIREMENT
ARAR
lYff*
Action to conserve endangered
or threatened species.
Applicable
Wetlands
40 CFR Pari 6, Appendix A
Actions must minimize the
destruction, loss, or
degradation of wetlands. as
defined by Executive Order
11990. Section 7.
Applicable
40 CFR Paris 230. 231
Actions must not discharge
dredged or fli material Into
wetlands without permit.
Applicable
Area affecting stream or river.
40 CFR 6.302
Action must protect fish or
wldllfe.
Applicable
* The ARAR types designated reflect the application status of each requirement when preparation of this 1M/IRA began.
In response to these requirements, Investigations were performed and the restMs are Indicated In the Comments column
which reflect the lack of any location-specific ARAR requirements which would preclude the proposed activity.
eyAg\.J
""'\lbI-."
COMMENTS
Proposed activities wli not
adversely affect endangered or
threatened species. Refer to
Section 2.2.5 and 7.3.
Proposed activities wli not
adversely affect wetlands.
Refer to Sections 2.2.6 and
7.3.
Proposed activities will not
adversely affect wetlands.
Proposed action wII be
protective of potentially
affected fish and wIdIne
resources. Refer to Sections
-------
:...:~,...".:
.:...."""
..,.,
, .~2
'~~ :
-------
~
..
SUR1=ACE WATER I~RlIA REIAEOIA:' ACTION PLAN
~KV O:..,4TS "LAN:. GO~E"'. COLOI'\AOO
1'9&; ~'r.D' .-aJnUt', agpenC.Qgt
APPENDIX F
CALCULATION SPREAD SHEET
-------
TABLE F-1
FLOW WEIGHTED MAXIMUM CONCENTRATIONS
(1) FLOW WE I GHTED FLOW WEIGHTED ~
SW.61 SW059 AVERAGE MAX I MUM
ANALYTE AltAR (Fl~ : 37.5 GPM) (Flow. 4.5 GPM) CONCENTRAT ION CONCENTRAT ION
===_==8Z..=...8:8....=..sz.....=aa=.. ........................ .....a........:........ a.......=-==.. .......c..:==
VOLATILE ORGANICS (2) (3)
(Concentrltion units. ue/l) C IVI C -x C IVI C 8U 4
...........................-......--- .......---. ....-....... -.........- .....-..---
Vinyl Chloride 2 6 15 5 10 6 14
Methylene Chloride (4,5) 5 U 7 44 3 5 1 40
Acetone (4,5) 10 U 13 130 6 13 12 111
1,1-Dichloroethene 7 7 143 21 133 9 142
1,1-Dichloroethl~ (5) 5 U 3 6 3 6 3 6
1,2-DiChloroethene (totll)(5) 5 U 3 5 10 56 4 10
Ch l oroforll 1 U 18 79 38 82 20 79
Clrbon Tetrlchloride 5 24 173 284 605 52 219
Trichloroethene 5 29 140 98 - 260 36 153
Tetrlchloroethene 1 U 39 280 94 270 45 279
DISSOLVED METALS
(Concentrltion units. ../l) C IVI C 8U C IVI C _x
...-.............-.-................-. ....-----.- ............ ........... ...........
Bery lli l1li (Be) 0.005 U 0.0026 0.0053 0.0025 0.0050 0.0026 0.0053
Mlne,""e (Mn) 0.050 0.1014 0.6430 0.0144 0.0461 0.0921 0.5790
Strontil.lll (Sr) (6) 0.396 0.1936 0 . 8000 0.5650 1.1700 0 . 2334 0.8396
Tin (Sn) 0.100 0.0797 1 .0000 0.0500 0.1000 0.0765 0.9036
TOTAL METALS
(Concentrltion Units. me/l) CIvil C _x CIvil C 118X
.................-..........---.--.-- ........... ............ ......-.... .......-...
Al""i,.. (Al) 2.000 U 3.9927 25 .4000 6.6908 22.8000 4.2817 25.1214
AntillOny (Sb) (5) 0.064 U 0 . 0309 0.0611 0.0403 0.1020 0.0319 0.0655
Baril8 (81) 1.000 0.2283 2.0200 0.2094 0.4610 0.2263 1.8530
Beryll il8 (Be) 0.100 U 0.0051 0.0572 0.0037 0.0076 0.0050 0.0519
C-*,illll (Cd) 0.010 0.0030 0.0142 0.0025 0.0050 0.0029 0.0132
ChrC8illl CCr) 0.050 0.0151 0.2120 0.0090 0.0232 0.0144 0.1918
Coealt (Co) 0.050 U 0.0295 O. 1320 0.0250 0.0500 0.0290 0.1232
Copper (Cu) 0.200 0.0271 0.2930 0.0215 0.0446 0.0265 0.2664
Iron (Fe) 1.000 12.0000 204.0000 5.7857 17.0000 11.3342 183.96,(,3
Lead (Pb) 0.050 0.0140 0.2150 0.0124 0.0317 0.0138 O. 1954
Li th i 11ft (l i) 2.500 0.0533 0.1520 0.4608 2.5600 0.0970 0.4100
Manglnne (Mn) 1.000 0.3603 3.6800 0.0723 O. 1970 0.3294 3.3068
Mercury (HII) 0.002 0.0002 0.0024 0.0002 0.0006 0.0002 0.0022
Mo l ybderuI (Mo) 0.100 0.0561 0.1740 0.0449 0.0191 0.0549 0.1514
Nickel (Ni) 0.200 0.0294 0.2460 0.0200 0.0400 0.0284 0.2239
Seleni"" (Se) 0.010 0.0026 0.0059 0.0044 0.0160 0.0028 0.0070
Stront;1II (Sr) (6) 0.382 0.2317 0.8000 0.6096 1 .3600 0.2722 0.8600
Vlnadilll (V) 0.100 0.0499 0.5550 0.0347 0.0595 0 . 0483 0.5019
-------
TABLE F-1 (Cont)
FLOW WEIGHTED MAXIMUM CONCENTRATIONS
'4 (1) FLOW WEIGHTED FLOW WEIGHTED
SW-61 5..059 AVERAGE MAX I MUM
ANALYTE AW (Flow. 37.5 GPM) (Flow. 4.5 GPM) CONCENTRATION CONCENTRATION
S====Z8S:C......-=....."........".. ........................ ......&8...........".. .........:... ............s
DISSOLVED RADIONUCLIDES
.. (Concentrltion units. pCi/l) C IV; C IIIX C IV; C IIIX
___.a_....................".-..."--.. .....-...... .-..--...... ........... ----.......
Gross Alpttl 11.00 3.800 20.600 11.000 16.000 4.571 20.107
Gross Beu 19.00 10.000 43.100 5.100 8.240 9.475 39.901
Totel Ur8nilAll 10.00 4.900 10.260 6.600 7.500 5.082 9.964
TOTAL RADIONUCLIDES
(Concentrltion units . pCi/l) C IV; C IIIX CIV; C IIIX
...........---....---................... .......-.-.. --........... ............ ----.......
Gross Alpttl 11.00 73.000 780.000 96.000 310.000 75 .464 729.643
Gross BeU 19.00 56.000 510.000 96.000 340.000 60.286 545.357
Plutonh.lll 239, 240 0.05 0.320 3.300 0.750 3.100 0.366 3 . 27'9
AIIIricil.lll 241 0.05 0.083 0.440 0.300 1.300 0.106 0.532
Toul UrenilAll 10.00 5.500 11.100 7.900 16.600 5.757 11.689
TOTAL INORGANICS
(Concentrltion Units . II1II/1) CIV; C IIIX CIV; C _x
.....a..............."................. .......--.... ....-e........ ............ ...........
Totll Dissolved Solids 400 411.0 3300.0 477.0 580.0 418.1 3008.6
(1) Collection It SW-61 includes flows f,.Q8 su,.fece IIIItl,. stetiona SW056, SW06O, SW061 end SW101.
(2) C IV; . Ave,.l;e Anelyte Concent,.ltion. Fo,. I 8"~ of stltiona (e.;. South Wilnut C,.eek) C IV; is c~ted by first
deuI'8ining the I,.it"-tic lIIen concentrltion It inc:lividu81 stltiona end then using this dltl to c~te till Iritll-
_tic lIIen for the stltions in thl 8"~' If I dltl.ll inc:licltn non-detected (i .1. 'U' desi;netion), the vilue usld
in c~ltion of the Irith8etic .." is one-hllf the Contract Required Detection Limit (CRDL). In cases wIIe,.e I
union or 8"~ of sutions hIS 8InY non-o.tec:t results in Iddition to one 0,. lIO,.e results below the detection Ii.it
for I contlinment, the cllculltld C avg ..y be ;reete,. then C IIIX.
(3) C 18X . Mlxi- Anelytl Concentrltion. C IIIX
st.tion or ;r~ of stltions. If thl .".lytl
C _x is set 1qI.!81 to..%hl.CRDL.
is thl lIIXi- o.tectld concent,.ltion in tile enti,.e dltl set for tile
is not o.tectld (i.e. 'U' desi;nltion) in II\Y of the station s~les,
-------
-------
~
~
S;;I'I~ACE WATER INTERIM REMEOI~ ACTION PlAN
'O::oEN. COI.ORAOO
89&;', ...rap . 1W8Inut . aDoenc .1)91
APPENDIX G
RISK ASSESSMENT CALCULATIONS
-------
South W86nut Cr... 688in
Surf... Wilt. Tr.at....t
Fugati"e Dust during construction
E~lUre of the PubLic
Risk CalcuLation Worksheet
ConstantS:
. .
Ac1Il t Bodv wei;tlt
Child Bodv weight
Ac1Ilt Inhalltion Rite
Worker Inhalltion Rate
Child Inhalation Rate
Operationing Rel...e Plr...ters
Exposure TI-
Exposure Fr~
Ac1Il t Exposure Duration
Youth Exposure Duration
Child Exposure Durltion
Av.rlling fI- (carc.)
AQ.ilt AVI TI- (non-carc.)
Child AVI Time (non-carc.)
Publ ic DI..-rsion Factor
Carcinogenic: (g)
Arsenic
Beryll iUl
Bis-(2.ethylhexyl)pftthallte
C"i UI
ChrOiliUl
Nickel
Totll
Non-clrcinogenic:(I)
Bis-(2.ethylhexyl)pftthllat.
BariUl
ChrOiliUl
Mercury
14.",."...
Total
Radioruclides:
Ur.,iUl
",-riciUl
Pll.ltoniUl
Totll
kg/..
~kg
~..
1113/.l
See Per IU n
Chi over Q
Airborn Dust
Conatr. Arel
Dust Source
JaD DUrition
Soil
Cone
(1liii/kg)
2.64E+03
1 . OOE+OO
1 .95£.00
3.001:.00
5.33(+00
4.70E+03
Soil
Cone
(III/kg)
1.95E.oo
4.1OE+01
5.331.00
1.001-01
1.301+02
BWa
BYe:
IRI
IRIII
IRc
1.ooE-06
1. ooE+03
1.ooE.03
1.00E-06
60
10
15
0.83
1.4
0.625
ET
EF
EDa
EDy
EDc
ATc
ATna
ATnc
8
60
1
o
1
25550
365
365
1.4oe-06
NA
1.0
4.20E-0l0
1.00
~PPENDIX G
PAGE 1 OF 9
Written: 09-J8n-91
Al.lthor: DCPalmer/~Kerri8an
Printed: 09-Jln-91
~i
kg
kt
Cubic meters/hour
Cubic meters/hour
Cubic meters/hour
Hours/day
Days/year
Years
Yelrs
Yelrs
DIY8
Days
Days
see/cubic meter
lilt/cubic meter
ecrn
kg/see
Yelrs
Source
(1liii/see)
1.11E.oo
4.20E-0l0
8.19E-04
1.26E-03
2.24e-03
1 .97!+OO
Source
RfC/lfD (1IIII/see)
2.00E-02 (e) 8.19E-04
1.DOE-03 (I,b) 1.98E-02
4.00E-06 (I,C) 2.24e-OJ
8.4OE-05 (I,C) 4.20E-05
1.14E-04 (I,b) 5.44E-02
~
----.-Ac1Ilt-..----
Air Cone Intlke Risk
(II1II/113) (IIIII/kt.day)
1.55£-06 3.47!-10
5.88E-10 1.32E-13
1.15£-09 2.56£-13
1.76£-09 3.95E-13
3.13£-09 7.01£-13
2.76E-06 6.18(.10
CItiId
Lifetime
Risk
Slope Factor
SF
5.00E+01 (b)
8.4OE+OO (b)
1.40E-02 (d)
6.10E+OO (b)
4.1DE+01 (b)
8.4DE-01 (b)
SoH
Cone DCf(f)
(uct/va) (...uct)
2.20E-05 1.3OE+05
3.001-06 5.201+05
1.IlOl-05 3.3OE+05
4.3OE-05
Source
(UCi/sac)
9.24e-06
1.26E.06
7.56£-06
1. 74E.08
1.10E.12
3.59E-15
2.41E-12
2.87E-11
5.19E.10
1. 79£-08
6.0SE-OS
3.S7!-12
1.26E-'1. .
B.1.2E-12
1.01E- '0
1.S2E.09
6.27!-OS
.-.---Ac1Ilt-.---.- --.-'-Child------
.Air Cone Intlke Risk Intake Risk
(l1li/113) (II8Itt/day) (lIIt/kt/dIY)
1.15£-09 1.8OE-11 8.98E-10 6.28£.11
2.7?E-08 4.33E-10 4.33£.07 1.52E-09
3.13E-09 4.91E-11 1.23E.05 1.72E-10
5.88E-11 9.21E-13 1.10E.08 3.22E-12
7.62£-08 1.19E-Q9 1.05£-05 1..1SE-09
2.32£-05
3. 'IoE-09
1.52E-Q6
Io.29E-05
3.8/.E-OS
3.66E-05
8.1'E-QS
Air Cone
(UC 1/11\3)
1.29!-11
1. 76E-12
1.06£-11
.---.-Ac1Ilt.------
Intake DOS.
(UCi) (l1li'8)
5.17!-09 6. 73E-Olo
7.06£-10 3.67E-0l0
4.23£-09 1.40E-03
2.104£-03
(I)Subchronic Inhalation RfC Vllues ucilized-
(b)lnhllltion value trOll IllS.
(c)lnhalltion vllue trOll HEAST, 4th Quarter, FY 1990.
(d)Orll vllue frOil IllS.
(e)Subchronic RfD value tra HEAST, 4th Quarter, FY 1990. AfC not IVlillble.
(f)lntemal Dosa Conversion Factors trOll DOE/EN-0071.
(g)Mluls inch8d in risk analysis include only thosa lIhich hi'" Slope hctors or UCs IVli llble.
Oust Source. (1.2 tona/acr.-lIOnth . ConatNCtion Ar.. / (30 . 24 . 3600» . 2000 lb\ton. .4536 kt/lb
Source. Dust source. Soi l Coneltltrltion
Air concentrltion . source. (X/Q)
Intlte . (Air coneentrltion . IR . ET . EF . ED) / (BY . AT)
Risk (for cancer) . Intlte . Slope Fector
Risk (non-cancer) . Intlte / RfC or RtO
Intlte (rldioruclides) . lir coneltltrltion . II . E1 . EF . jaD Q.iretion
-------
South Walnut Cr.ek 88ain
Surfac. Wlt.r Tr.lt_t
Fugitive Dult ~r;ng construction
Exposurl of Construction Workers
~iSK Caiculation Worksn88t
Constants:
..J
..
.
"dul t Body Wei gilt
Child Body Weight
Adult Innllition .Itl
Worklr Innilition .Itl
Child Innilltion .Itl
Operationing .elilse Plr...ters
EJq:I08Ure T 1-
Exposurl Fr..."cy
Adult Exposure Ourltion
Youth Exposure Ourltlon
Chi ld Exposurl Ourltion
AVlrlgi", Ti.. (Clrc.)
Adult Avg Time (non'clrc.)
Child Avg Ti.. (non-clrc.)
Worker Dispersion Factor
Carcinogenic: (g)
Arsenic
Seryll i ~
Sis-(2-ethylhexyl)phthllltl
Caanillll
ChrOllli~
Nickel
Totll
Non'clrcinogenic:(g)
Sis-(2-lthylhlxyl)phthllate
SlriUII
ChrOllli~
Mercury
MlnglnHl
Toul
Rldionl.lClidls:
UraniUII
Amt,.; C i UII
Plutoni~
Toul
kg/1111
8l1li kg
8l1lil1li
1113/lll
See Per Min
CI'I i over Q
A I rborn Oust
Canstr. Arll
Oust SourcI
Job Ourltion
Soil
Cone
(till/kg)
2.~+03
1.00£+00
1.95E+OO
3. OOE+OO
5.33E+00
4.70E+03
8W8
8we
1.1
Ih
I.c
1.00E-06
1.00E+03
1. 00£'03
1.00E-06
60
70
15
0.83
1.4
0.625
~PPENDIX G
PAGE 2 OF 9
Writtefl:
Autnor:
Printed:
09'Jan-91
OCPalrner/ICJ(
09'Jan.91
£T
EF
EOI
EOy
£Oc
ATc
ATne
ATnc
1
60
1
NA
NA
25550
365
NA
kg
kg
Cubic metlrs/hour
Cubic metlrs/hour
Cubic ..tlrs/hour
Hours/day
Olva/Yllr
Yllr.
Yelr.
Yel'"
Diva
DIva
DIva
see/cubic metlr
1118/a.Dic ..ur
acr..
lei/see
Yllrs
SourCI
(III/lee )
NA
NA
NA
NA
NA
NA
Soil
Cone
(-.lleg) RfC/RfOCI)
1.951+00 2.oar-02 (I)
4.1OE+01 1.00r-Q3 (I,b)
5.33£+00 4.00E-06 (I, c)
1.oar-01 1.4OE-OS (I,C)
1.301+02 1.141-04 (I,b)
------Adult-----_.
Air Cone Intaitl .isk
(111/111) (lIIIkg-dly)
1.32£-02 2.95E-06
5.0QE-06 1.1ze-09
9.15E-06 2.18E-09
1.5DE-OS 3.35£-09
2.671-OS 5.96E-09
2.35E-02 5.26E-06
1.47!-04
9.39£-09
3.05E-11
2.05£'08
2.44E-07
4.41E-06
1. 52E-04
------Adult.------
Air Cone Int.1 .Isk
(-.183) (III/kllday)
9.15£'06 1.53E-07 7.631-06
2.35E-04 3.68E-06 3.68E-03
2.671-OS '.1?E-07 1.04E-01
5.00!-07 7.S3E-09 9.3ze-05
1.08E-01
Air Cone
(uCl/lI1)
1.1or-07
1.50£-08
9.00E-08
'--'--Adult-..-..-
Intakl DOlI
(uCl) (1Ir.)
4.4OE-05 5.72E+OO
6.00E-06 3.12£+00
3.60£-05 1.19£+01
2.07!+O1
NA
5
NA
NA
1.00
Slope Factor
SF
5.00E+01 (b)
1.4OE+OO (b)
1.40(-02 (d)
6.10£+00 (b)
4.10£+01 (b)
1.40E-01 (b)
Soil
Cone OC'Cf)
(uCl/tIII) (.....,uCl)
2.20£-05 1.30£+05
3.00r-06 5.20E+05
1.eor-05 3.30£+05
4.30£-05
SourcI
(-.lsee)
NA
NA
NA
NA
SourCI
(uCi/IIC)
NA
NA
NA
(I)Subctlronic IMIlltton UC velues utilized.
(b)lnnllation vllue fr08 IRIS.
(c)lnhllltlon vllue fr08 HEAST, 4th Quarter, FY 1990.
(d)Orll vIlue fr08 IRIS.
(e)Subchronic UO velue fr08 KEAST, 4th GuIIrtlr, FY 1990. UC not IVli lable.
(f)lnternel 0088 Conversion Factors fr08 DOE/EN-007'.
(g)Metlls included in risk anelyais i~lud8 only thOle Which hive Slope Factors or .fCs aVlilable.
Air concentrstlon . Soil concentrltion . lirborn dust . kg/III
Intlkl . (Air coneentrltion . IR . ET . £F . ED) / (BW . AT)
Risk (for canelr) . Intlkl . Slope Factor
Risk (non-canelr) . Intlkl / RfC or RfO
Intlke (rldionuclidts) . lir coneentrltlon . I. . £T . EF . job durltion
-------
~ISK Calculatlon worksheet
Cons tints:
Adul t Body Weignt
Child lody Weivftt
Adult Innilition Rite
Worker Innilition Rite
Child InIIllltion Rite
Operltioning Rele..e Plr...te...
Exposure TI-
Exposure Frequency
Adul t Expoaure Durltlon
Youth Exposure Duration
Child Exposure Duration
Averaving TI- CClrc.)
Adul t Ave TI.. Cnon-clrc.)
Child Ave Ti.. Cnon-care.)
Worker Dispersion flCtor
Carcinoeenie:cv)
Arsenic
Beryll iUl
lis-C2-ethylhexyl)phthallte
CacaiUl
ChrOlliUl
Nickel
Totll
Non-clrcinovenic:c,)
lis-C2-ethylhexyl)phthllate
BariUl
ChrOlliUl
Mercury
Manganese
Totll
Rldionuclidn:
Uranil.8
All8ricilAl
PlutoniUl
ToUl
South Wlllnut Creek e..in
Surface Wat- Treat.....t
Fuvative OUSt duril'lf cOt'l8truction
Expoaure 01 Other Site Workers
ke/..
8l1li ke
gill...
1113/8l
See Pel' III n
..
Chi over Q
A i rbo,." Dus t
Constr. Are,
Dust Source
JoD Durltion
Soil
Cone
Clll/k,)
2.64E+03
1 . OOE+OO
1 .95E+OO
3.00£+00
5_33E+oo
4.1OE+03
IWa
BWe
IRa
I'"
IRc
1.00E-06
1.00E+03
1.00E-03
1.00E-06
60
70
15
0.83
1.4
0.625
ke
ke
Cubic ..ters/hour
Cubic ..t,rs/hour
Cubic ..t,rs/hour
Hourl/dly
Days/year
Yeara
Y'I'"
Yee...
DIYS
DIYS
DIYS
see/Mlc ..tel'
l118/cubic ..tel'
acr..
ke/lee
Yea...
Source
Cllllsee)
1.11E+OO
4.20E-04
8.19£-04
1.26(-03
2.241-03
1 .97E+OO
Soil
Cone Source
Clllk,) atC/R1OCa) CII/lee)
1.95E+OO 2.00E-02 Ce) 8.19£-04
4.1OE+01 1-001-03 CI,b) 1.981-02
5.33e+OO 4.001-06 Ca,c) 2.241-03
1.DOE-01 8-401-05 Ca,c) 4.201-05
1_3OE+02 1.141-04 Ca,b) 5.44(-02
ET
Ef
EDa
EDy
EDc
ATc
ATne
ATnc
8
60
1
o
1
25550
365
365
2.43E-04
IIA
1.0
4.20£-04
1.00
Slope factor
SF
5.001+01 Cb)
8.40E+OO Cb)
1.401-02 Cd)
6.10£+00 Cb)
4.10E+01 Cb)
8.40E-01 Cb)
SoH
Cone DCFCf)
CI.£I/II) CIIr.,~t)
2-201-05 1.3OE+05
3.001-06 5.20E+05
1.801-05 3.301+05
4.301-05
Source
(~I/.8C)
9.24E-06
1. 26E-06
7.56E-06
APPENDIX G
PAGE 3 OF 9
Written:
Author:
Printed:
09'Jan-91
OCPllmer/((errigan
09-Jln-91
~
6
------Adult---.---
Air Cone Intake Riak
CIIIIII83) Clll/k,-d8y)
2.691-04 6.03(-08 3.01E-06
1.0ZE-07 2.28E-11 1.92£-10
1.991-07 4.45E-11 6.23E-13
3.061-07 6.85E-11 4.1IE-10
5.44(-07 '1.22£-10 4.991-09
4.8OE-04 1.07!-07 9.01E-08
3.11E-06
'-----Adult-------
AII' Cone Intlke Risk
C..,83) Cllllllklldly)
1.991-07 3.12£-09
4.8OE-Q6 7.52£-08
5.44(-07 8.52£-09
t.02£-08 1.6OE-10
1.32£-05 2.07E-07
1. 56E-07
7.52£-05
2.13E-03
1.9OE-06
1.82£-03
4.02E-03
------Adult-------
Intake 008e
(~I) Cmr.)
8.98(-07 1.17E-01
1.22£-07 6.37E-02
7.35E-07 2.42£-01
4.23E-01
(I)Subchronic Inh,lation afC values uttllzed.
(b)lnnllation value fr08 IRIS.
(c)lnnalation value 11'08 HWT, 4th Gulrtlt', FT 1990.
(d)Orll value 11'011 IRIS.
(,)Subc/lronic R10 value fr08 MEAST, 4th Gulrtlt', F" 1990- Rte not available.
(1 )OO8e ConYers i on FlCto,.. 11'08 00E/EM-0071.
Ce)Mltlls included in risk anelysis include only those with Slope FlCto... or atcs available.
OUSt Source. (1.2 tona/lCre-8Onth . CONtructlon AI''' I C30 . 24 . 3600» . 2000 lb\ton . .4536 ke/lb
Source. Dust source' Soi l Concentrnion
Air concentration. source' CX/Q)
InUke. {Air coneentratlon . II . ET . EF . ED> / (8'" . AT)
Risk (for caneer) . Intlke . Slope FlCtor
Risk Cnon-caneer) . Intlke / RtC or 110
Intak, Cr8dionuclidn) . air concentration' IR . E! . EF . job duration
Dose Crldionuclides) . Intlke . DOle Conversion FlCtOr (DCF)
Air Cone
(~I/a1)
2.25E-09
3.06E-10
-------
~isk CalcuLation Worksheet
Constlnts:
-..J
'.
..
A<*.II t Body wei;ht
Child Body Weight
A<*.Ilt Innilition Alte
Worklr Innilition Rltl
Child Innilition altl
Operltioning AIIII.I Plr...ters
Exposure TIN
Expo.ure Frequency
A<*.Ilt Expo.url Durltlon
Youth Exposure Durltion
Child Expoaure Durltion
AVlraging Time (carc.)
A<*.Ilt Avg TiN (non-clrc.)
Child Avg TiN (non-clrc.)
Public Dispersion FlCtor
Carcinogenic:
Carbon Tltrlchloride
ACltone
1,1-Dichlorlthene
1,2-Dichlorolthene
TetrlchlorOlthene
Trichlorolthene
Methylene Chloride
Vinyl Chloride
1,1 DichlorOlthane
Carbon Disulfide
Touls
Non-carcinogenic:
Carbon Tltrlchloride
Acetone
1.1'Dichlorethene
1.Z-DichlorOlthene
TetrachlorOlthene
Trichloroethene
Methylene Chloride
Vinyl Chloride
1,1 DichlorOlthane
Carbon Disulfide
Totlll
South Walnut Cr..k e..in
SUtflee Wlter Tr..tMent
Collection Tlnk V8f'lting
Exposure of the Public
Liter Per GII
Sec Per Nin
A
N/V
kg/1118
8111 kg
gill! 1118
1113/1111
Chi over a
JoO Durltion
Flow Altl
Vapor
Cone
(1118/1 )
1.97E-05
O.OOE+OO
1. 16E-05
1.69£-06
4.13E-06
9.41E-06
O.OOE+OO
O.OOE+OO
3.021-06
O.OO!+OO
1.10E-04
Vepor
Cone
(1118/1 )
1.971-05
O. OOE+OO
1. 16E-05
1.69£-06
4.131-06
9.41E-06
O. OOE+OO
O. OOE+OO
3.0a-06
O.OOE+OO
1.10E-04
aWa
BWe
IAI
IRw
IRc
3.7853
60
62.37
3.28E+01
1.00E'06
1 .00e+03
1.00e-03
1.00E'06
70
15
0.83
1.4
0.625
rrmHg L/;mole IC
APPENDIX G
PAGE 4 OF 9
Written: 07'Jan-91
Author: OCPalmer/(lCerrigan
Printed: 08'Jan.91
kg
kg
Cubic NterS/hour
Cubic Nters/hour
Cubic Nters/hour
'---"A<*.Ilt..-....
Air Cone Intakl Risk
(1118/113) (lII8/kg/dly)
1.04C-10 9.29£-12
O.OOE+OO O.OOE+OO
3.19£-10 3.31£-11
8.981-12 1.99£-13
2.191-11 1.94E-12
4.99£-11 4.43E-12
o . OOE+OO O. OOE+OO
Q.OOE+OO O.OOE+OO
1.60£-11 1.42£-'2
O.OOE+OO O.ooE+OO
'.21E.12
O.OOE+OO
5.66E-11
O.OOE+OO
4.9Oe-15
1.05E-13
O.OOE+OO
O.OOE+OO
o . 00E+00
O.OOE+OO
5.80E-11
Chi ld
Lifetime
Risk
2.39E'12
O.OOE.OO
8.03E'11
O.OOE+OO
6.9'£- 15
1.'9E'13
O.OOE+OO
O.OOE+OO
O.OOE+OO
o.ooe+oo
8.28E-11
'.----A<*.Ilt..---.. """Child......
Air Cone Intake Aisk Intake Risk
(1118/1113) (.../kg/day) (mg/kg/dly)
1.04E-10 2.17E-'1 3.10E-08 7.SSE-11 1.08E'07
O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO O.OOE.OO
3.19£-10 7.81£-'1 8.14E.09 2.75E-10 3.06E'08
8.98E-12 '.86E-12 9.32E-11 6.52E.12 3.26E'10
2.191-11 4.54E-12 4.54E-'0 1.59£-11 1.59E-09
4.99£-11 1.03E-11 NA 3.62E-11 NA
O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO O.OOE.OO
O.ooE+OO O.OOE+OO NA O.OOE+OO NA
1.6OE-11 3.32£-12 3.32£-'1 1.16£.11 1.16E-10
O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO O.OOE.OO
4.03E-08 1."1E'07
(a)Chronic Oral A10 utilized whlre Chronic Inhalation AfC not available.
(o)lnhllation value fraa IRIS.
(c)lnnalation value fraa HEAST, 4th Quartlr, FY '990.
(d)Oral value fraa IRIS.
(e)Oral value fraa HEAST, 4th Quartlr, FY 1990.
(f)Value not IVlilabll on IRIS.
ET
EF
EDa
EDy
EDc
ATc
ATI'I8
ATne
24
265
30
25
5
25550
10950
1825
1.40E-06
IIA
60
Hours/day
Oays/year
Years
Years
Y..rs
Oays
DIYS
Days
see/cubl c I118ter
Years
gJ8
Source II Vapor concentration. flow rltl . I itlrs per glllon/slConcis per minute
Air concentrltion II sourci . (X/a)
Intakl II (Air concentrltion . IR . ET . EF . ED> I (BW . AT)
Risk (for cancer) II Intake. Slope Flctor
Risk (non-canclr) . Intake I RfC or RfD
Slope Factor
SF
Sourci
(I118/SIC )
1.30E-01 (b) 7.46E-05
NA O.OOE+OO
1.20E+00 (b) 2.71e-04
NA 6.42e-06
1.8Oe-03 (c,f) 1.56£-05
'.7OE-02 (c,f) 3.56E-05
1.40E-02 (0) 0.00£+00
1.9Oe+oo (1,1) O.OOE+OO
IIA 1. 'loE-05
IIA 0.00£+00
RfC/R1O(I)
Source
(1II8/11C )
1.00£-04 (I,d) 1.46E-05
1.00E-01 (I,d) 0.00£+00
9.00E-03 (I,d) 2.11E'04
2.00e-02 (a,d) 6.42£-06
1.00E-02 (I,d) 1.56E-05
IIA 3.56E-05
9.00e-01 (c,f) 0.00£+00
IIA O.OOE+OO
1.00E-01 CC,f) 1.1'E-05
3.00E-03 (c,f) O.OOE+OO
-------
South W..,ut Creek a.ain
Surface Water Treatment
Collection rink Venting
Exposure of RFP Workers
Risk Calculltion Worksheet
Cons tints :
Adul t Body Wei ght
Child Body Wlight
Adult Inhelltion Rate
Worker Inhalltion Rate
Child Inhalation Rate
Operltioning Rele..e Par...ters
E~ure Ti.
. E~ure Frequency
Adult Exposure Duration
Youth Exposure Duration
Child Exposure Duration
Averaging TI. (carc.)
Adult Avg TI.. Cnon.care.)
Child Avg TI.. (non-care.)
Worker Dispersion Factor
Li tar Per Gal
See Per Min
R
N/V
kll/1111
glll/kg
gllllIII
m3/ml
Chi over Q
Job Duration
Fla.. Rate
BWa
Bwe
IRa
Ib
IRc
3.7853
60
62.37
3.28E+01
1.00E.06
1.00E+03
1.00E-03
1.00E-06
70
15
0.83
1.4
0.625
APPENOIX G
PAGE 5 OF 9
Written: 07'Jan-91
Author: OCPalmer/((
Printed: 08'Jan-91
IIIIIHg 1/8Il1O I e K
~
ET
EF
eoa
EDy
EDc
ATc
ATna
ATne
24
265
30
25
5
25550
10950
1825
2.69£-05
IIA
60
kg
kg
Cubic meters/hour
Cubi c meUrs/hr
Cubic meters/hour
4
Hours/day
Dava/year
Years
Ylars
Yeers
Davs
Dava
Days
SIC/Mic meter
Years
gP8
Carcinogenic: Sl~ Factor
Cone SF Sourci Air Cone Intake Risk
(l1li/ I) C II1II SIC) (l1li/113) (JIll/kg/day)
Carbon Tetrachloride 1.97!-05 1.30E-01 Cb) 7.fo6E-05 2.01E-09 1.78E-10 2.32E-11
ACltone O. ooe.oo IIA O.OOE.oo O.OOE.oo 0.00£+00 O.OOE+OO
1,1-0ichlorlthene 7.16£-05 1.20E+OO (b) 2.71E-04 7.29£-09 6.48E-10 7.rn.10
1,2-DichlorOithene 1.69£-06 NA 6.42£-06 1.73E-10 1.53E-11 O.OOE+OO
Tatrachlorolthene 4.13E-06 1.80E-03 (c,f) 1.56£-05 4.20E-10 3. 74E - 1 1 6.72E-14
Trichlorolthene 9.41E-06 1.70E-02 Cc,f) 3.56£-05 9.5.-10 8.52E-11 1.45E-12
Mlthylene Chloride O.OOE+OD 1.40E-02 (b) 0.00£+00 O. OOE.oo O.OOE+OO O.OOE+OO
Vinyl Chloride O.OOE+OO 1.9OE+OO (e,f) 0.00£+00 O.OOE+OO O.OOE+OO O.OOE+OO
1,1 DichlorOithane 3.0ze-06 IIA 1.14£-05 3.08E- 10 2. 74E- 1 1 O.OOE+OO
Carbon Disulfide O.OOE+OO IIA O.OOE+OO 0.00£+00 O.ooE+OO O.OOE+oo
Totals 1.10E-04 8.02E- 10
Non-carcinogenic:
Cone RfC/RtO(a) Source Air Conc Intake Risk
CIIII/1) C l1li/ SIC) (II1II113) CIIII/kg/day)
Carbon Tetrachloride 1.971-05 7.00£-04 (a, d) 7.fo6E-05 2.01E-09 4.16£-10 5.95E-07
ACltone O. OOE+OO 1.00£-01 CI,d) 0.00£+00 O.OOE+OO 0.00£+00 O.OOE+OO
1,1-Dichlorlthene 7.161-05 9.00E-03 Ca,d) 2.71E-04 7.29£-09 1.51E-09 , .68£-07
1,2-DiclllorOithene 1.691-06 2.00£-02 Ca,d) 6.t.2E-06 1.73E-10 3.58£-1' 1.79£-09
TetrlchlorOithene 4.131-06 1.00E-02 (a,d) '.56£-05 4.20E-10 8.72E-11 8.72E-09
T ri ch lorOithene 9.41E-06 IIA 3.56£-05 9.5.-'0 1.m-,0 IIA
Methylene Chloride O.OOE+OO 9.00E-01 (c,f) O.ooE+OO O.OOE+OO O.OOE+OO O.OOE+OO
Vinyl Chloride O. OOE+OO IIA 0.00£+00 O.OOE+OO O.OOE+OO IIA
1,' DiehlorOithane 3.02E-06 1.00E-01 (e,f) 1.14£-05 3.08E-'0 6.39£-1' 6.39£-10
Clrbon Disulfide O. OOE+OO 3.00E-03 (c,f) O.OOE+OO O.OOE+OO O.OOE+OO O.OOE+OO
Totals 1.10£-04 7.74E-07
CI)Chronic Oral RtO utilized ~ere Chronic Inhalation RfC not available.
(b) Inhalation value fr08 IRIS.
(c) Inhalation value fr08 HEAST, 4th Quarter, FY '990.
(d)Oral value fr08 IRIS.
(e)Oral value fr08 HEAST, 4th Quarter, FY 1990.
Cf)Value not Ivailable on IRIS.
Source. Vapor concentration. flov rate. liters per gillon/seconds per minute
Air concentration. source. (X/Q)
Intake. (Air concentration. IR . E1 . EF . EO) / (BW . AT)
Risk (for cancer) . Intake. Slope Factor
Risk (non-cancer) . Intake / RfC or RfO
-------
-J,
~PPENCIX G
PAGE 6 OF 9
Vapor concentration calculation
Sou'h WlI6nut Ct... Be... Surf8C. W.ter Tr..'....n' Printed: 08- Jan-91
Collection rank Venting IIr; tten: 08-Jan-91
Author: OCPalmer
Liq Conc Molecullr g_8Dl"/l Liq .ole Vep Pres. Partill Pr. PP Frlct 'lap Conc
(1III/l) \/eight Friction (II'1II Hg) (II1II Hg)
Carbon retrachloride 2.191-01 153.84 1.42E-06 2.57E-08 91.17 2.34e'06 3.90e-09 1_97E-05
Acetone O.OOE+OO 58.08 O.OOE+OO O.OOE+OO 185.20 o.ooe+oo o.ooe+oo o.ooe+oo
1,1-Dichlorethene 1.4U-01 96.95 1.46E-06 2.64E-08 510.56 1.35e-05 2.25e-08 7.16e-05
1,2-0ichloroethene " 1-.00E-02 96.95 1.03E-01 1.86E-09 171. 69 3.20E-01 5.33e-10 1.6ge-06
retrachloroethene 2_7'9£-01 165.85 1.68E-06 3.04E-08 14.98 4.55e-01 7.58E-10 t,.13e-06
rri cftloroethene 1.53E-01 131;4 1.161-06 2.10£-08 62.28 1.31E-06 2.18E-09 9.t,1e-06
Methylene Chloride O.OOE+OO 84.93 0 . OOE+OO O.OOE+OO 351.86 O.OOE+OO o.ooe+oo o.ooe+oo
Vinyl Chloride O.OOE+oo 133.41 O.OOE+oo 0.00£+00 2819.28 O.OOE+OO O.OOE+OO o.ooe+oo
1,1 Dichloroethene 6.00E-03 98.96 6.06£-08 1.09£-09 510.56 5.59£-01 9.31E-10 3.02E-06
Carbon Disulfide O.OOE+OO 16.14 O.ooe+OO O.OOE+OO 306.22 O.OOE+OO O.OOE+OO O.OOE+OO
Water 0 18.02 5 .54£+01 1.000£+00 18.69 1.87E+01 3.12E-02 1.84e.01
ToUll O.OOE+OO 5.54£+01 6.00E+02
.
Gr..-lDOl.. per liter. (l iquid concentration I 1000) I molecular weight
Liquid 8Dle fraction. gr..8Dl.. per l iter I total gr"lIOl..
Partial pr..aure . v8f'Or prnaure . liquid 8Dle fraction
Partill ~r..sure fraction. pertial pr..aure I atl108pfteric pr..sure
Vlpor concentration. partial prnaure fraction. (II/V> . IIIOlecular ...ight
-------
~FPENCIX G
FAGE 7 OF 9
Vapo~ P~essure C~lcul~tion
Printed: 08-Jan-91
Written: 08-Jan-91
Author: DCPIlmer
T1 P1 T2 P2 T1(1C) T2(1C) (20-n )/(T2-T1) LOll P P
Carbon Tetrachloride 4.3 40 23 100 217.4 296.1 8.93E-01 1.96 91.17 ~
Acetone 1.1 100 39.5 400 280.8 312.6 4.1ee-01 2.21 185.20
1,1-0ichlorethene 14.8 400 31.1 160 281.9 3010.8 3.67E-01 2.11 510.56
1,2-0ichlorOithene 9.5 100 41 400 282.6 314. I 3.65E-01 2.23 111.69
TetrlchlorOithene '. .13.8 10 40.1 40 286.9 313.2 2.14E-01 1.18 14.98
Trichloroethene 11.9 40 31.4 100 285 3010.5 4.67E-01 1.1'9 62.28
Methylene Chloride '6.3 100 24.1 400 266.8 291.2 8.9ee-01 2.55 351.86
Vinyl Chloride -28 . 400 -13.8 160 245.1 259.3 3. 45E+OO 3.45 2819.28 .
1,10ichlorOithane 14.8 400 31_7 760 287.9 304.8 3.67E-01 2.11 510_56
Carbon Disulfide -5.1 100 28 400 268 301.1 7.89£-01 2.49 306.22
WaUr 11.2 10 22- 1 20 284.3 295.2 8.99£-01 1.21 18.69
LOll P . [log(P2/P1] . (T2/294.1> . [(20-T1)/(T2-T1)]+lO\1 P1
Vapor pressure (P) . 10-(lO\1 P)
-------
Risk Calculation workSheet
South WMwt Creek a..in
Surface WIlt... T,e.tMeftt
Influent Tink lupture (10,000 911)
Exposure of the Public
Constants:
J
Liter Per GII 3.7853
Sac Per lIin 60
R 62.37
N/V 3.28E+01
. . kg/III 1.00E-06
~kg 1.00E+03
l1lil1li 1.00E-03
1113/.l 1.00e-06
AQ,jlt BOdy weight BW8 70
Chi ld BOdy weight BWc 15
AQ,jlt Inhilition 'Itl I" 0.83
Worker Inhilition Rltl IR" 1.4
Child Inhilition Rltl IRC 0.625
Operltioning lele"l Plr...tlrs
Expoaure T 1- ET 24
Exposure Fr~ EF 1
AQ,jl t Exposure Durltion EDI 1
Youth Exposure Durltion EDy 0
Child Exposurl Durltion EDc ,
AVlrlging Time CClrc.) ATc 25550
AQ,jlt Avg Time (non-clrc.) AT". 365
Child Avg Time (non-carc.) ATne 365
Public Diaperaion FlCtor Ch i 0V8t' Q 1.271-03
JoD Duration IIA
Flow Rltl 6.9
Carcinogenic:
..
Carbon Tetrachloride
Ac.tone
" '-Olchlorlthane
1,2-Dichloroethane
Tetrachloroethane
Trichloroethane
lI.thylene Chloride
Vinyl Chloride
1,1 Dichloroethana
C.rbon Disulfide
Totala
Liquid
Cone
ClIIIIl)
2.19E-01 1.301-01 Cb)
0.00£+00 IIA
1.421-01 1.2OE+OO Cb)
1. 00E-02 IIA
2.19£-01 1.aoe-03 (c,g)
1.53£-01 1.1OE-02 Cc,g)
O.OOE+OO 1.40(-02 Cb)
0.00£+00 1.9OE+OO CI,g)
6.00e-03 IIA
O. OOE+OO IIA
8.09E-01
Slope FlCtor
SF
Non-carcinogenic:
Liquid
Cone
ClIIIIl)
2_19E-01
0_001+00
1.42!-01
1.0CII-02
2.7'91-01
1.531-01
O. OCII+OO
O. OCII+OO
6.0CII-03
0.001+00
8.091-01
UC/.fOCI)
Carbon T.trachloride
Ac.tone
',1'Dichlorlthane
1,2-0Ichloroethene
Tetrachloroethane
Trichloroethane "
Mlthylene Chloride
Vinyl Chloride
1,10lchloroethana
Carbon Disulfide
Totlla
IIIIIHg l/lIDOl. Ie
~PPENCIX G
PAGE 8 OF 9
written: 08'Jan.91
Author: OCPalmer/lClCerr;gan
Printed: 08'Jan'91
Itg
Itg
Cubic matlrl/hour
Cubic ..t.rl/hour
Cubic ..ters/hour
Houra/day
OIYS/Yllr
Ye.ra
Yllrs
Y..r.
Days
OIYS
DIYS
lac/cubic ..tel'
YHra
!PI
--'---Adult--..---
SourCI Air Cone Intakl Rilk
(nil/lac) (l1li/83) (lilt/ltg/day)
9.59E-02 1.zze-04 1.36£-09
0_00£+00 O-OOE+OO O.OOE+OO
6.zze-02 1.9OE-05 8.84E-10
4.381-03 5.561-06 6.zze-1'
1.zze-01 1.55E-04 1.741-09
6.70E-02 8.51E-05 9.52E-10
O.OOE+OO O.OOE+OO O.ooE+OO
0.00£+00 O. OOE+OO O. OOE+OO
2.631-03 "3.341-06 3.13E-11
O.OOE+OO O.OOE+OO O.OOE+OO
1.T7E-10
O.OOE+OO
1.06E-09
0.00£+00
3. 12E- 12
1.62£-11
O.OOE+OO
0.00&+00
O.ooE+OO
O.OOE+OO
1.26E-09
------AQ,jlt-------
Air Conc Intllte Rilk
(l1li/83) (l11/k,/day)
1.22£-04 9.541-08
O. OOE+OO O. OOE+OO
1.9OE-OS 6.18!-08
5.561-06 4.36E-09
1.55E-04 1.22£-01
8.51E-05 6.66£-08
O.OOE+OO O.OOE+OO
0.001+00 O.OOE+OO
3.341-06 2.61&-09
O.OOE+OO O.OOE+OO
(a)Subchronic Oral RfO utilized whirl SUbchronic Inhilition RfC not Ivailabll.
(b)lnhllation vllue frG8 IRIS.
(c)lMllltion value frG8 HEAST, 4th Quartlr, FY 1990.
(d)Orll. vllue frG8 IRIS.
(e)Orll vilue frG8 MEAST, 4th Quartlr, FY 1990.
(f)Subchronic vilue not IVIllabll; chronic vilue util izad.
(g)Value not IVlilabll on IRIS.
Sourci. Liquid Concentrltion . Flow Ratl . Litlr. par gillon / saconds per minute
Air concentrltion . source. (X/O)
Intake. (AII' coneentrltion . IR . ET . EF . ED) / (BW . AT)
Rislt (for cane.r) . Intlke . Slope Factor
Rislt cnon-caneer) . Intake / RfC or RtO
Sourcl
(l1111/alC)
1.00e-03 Ca,e) 9.59E-02
1.00E+OO CI,e) O.OOE+OO
9.oar-as CI,e) 6.22£-02
2_001-01 ca,l) 4.381-03
1.001-01 Ca,e) 1.221-01
NA 6.1OE-02
9-001-01 Cc,g) O.OOE+OO
IIA O. OOE+OO
1.00E+OO Cc.g) 2.631-03
3-DOE-03 (c,f,g) O.OOE+OO
1.W-05
0.00&+00
6.87!-Q6
2.18&-08
1.22£-06
ERR
0.00£+00
ERR
2.61E-09
O.OOE+OO
2.171-05
Child
Li fet ime
lIisk
6.20E- 10
O.OOE+OO
3.71E-09
O.OOE+OO
1.09£-11
S.66E-11
O.OOE+OO
O.OOE+OO
O.OOE+OO
O.OOE+OO
1o.100E'09
----"Child--"'-
Inulte Risk
(Illg/kg/day)
3.34E-07 '.77E-OS
O.OOE+OO O.OOE.OO
2.16£-01 2."E-05
1.52E-08 7.62E-08
'.25E'07 '.25E'06
2.33E-01 ERR
O.OOE+OO O.OOE.OO
O.OOE+OO ERR
9.15E-09 9.15E-09
O.OOE+OO O.OOE.OO
7.61E-05
-------
~isk Calculation Worksheet Soutll W.-wt Cr... Besill
Swof... w.tef Tr..t_t
Influent Tant Rupture <'0,000 g.l)
Exposurl 01 RFP Work Irs
Constants:
litlr Per G.l 3 . 7853
See Plr Min 60
R 62.37 IIIIIIIg l/gIIIOll IC
N/V 3.2SE+01
leg/III 1 .00E-06
gla/kg 1.00E+03
l11li1118 1.00E-03
1113/.l 1.00E-06 ..
Adul t Iodv we i gII t BWI 70 leg 4
Child Body Wlight BWe 15 leg
Adult Inhalation Rat. IRa 0.83 Cubic met Irs/hour
Worklr Inhilition .,t. IR.. 1.4 Cubic .tlrs/hr
Child Inhalation Rlt. IRc 0.625 Cubic .tlrs/hour
Operltioning Rill'" P.r...tlr.
EJIpoSure TI. ET 24 Hour./dly
~posur. Fr~ EF 1 DaYS/Y.lr
Adul t Exposur. Durlt I on EDI 1 Tllr.
Youth Exposun Durstion EDy 0 Yllr.
Child Exposurl Durltion EDc 1 Yell"
AVlrlging Ti. (clrc.) ATc 25550 DIYS
Adult Avg Time (non-clrc.) ATna 365 OIYS
Child Avg Tlma (non-clrc.) ATne 365 DIYS
Work II' Dlsper.ion Factor Chi over G 2.83E-02 see/cubic ..tlr
Job Durltion IIA Yelrs
FlOll Ratl 6.9 gP8
Carcinogenic:
Non'carcinogenic:
Li~id
Conc
(1IIg/ l )
2.191-01 1.301-01 (b)
o . 00£+00 IIA
.1.42£-01 1.20£+00 (b)
1.00£-02 ItA
2.79E-01 1.8OE-03 Cc,g)
1.531-01 1.70e'02 (c,g)
O.OOE+OO 1.4QE-02 Cb)
0.001+00 1.9OE+OO (I, g)
6.001-03 IIA
O. OOE+OO IIA
8.09!-01
liquid
Conc RfC/RfOCa) Sourci
C88/l) (.../see)
2.191-01 1.00E-03 Ca,l) 9.591-02
O.OOE+OO 1.00E+OO (1,1) 0.00£+00
1.421-01 9.001-03 (1,1) 6. 22E-02
1.001-02 2.001-01 CI,I) 4.381'03
2.791-01 1.001-01 (1,1) 1.22£-01
1.531-01 IIA 6.70e-02
0.00I+0O 9.001-01 (c,g) o.ooe+oo
0.001.00 IIA O.OOE+OO
6.001-03 1.001+00 (c,g) 2.631-03
O.OOE.oo 3.00e-03'(c,f,g) O.OOE+OO
8.09!-01
Slope FlCtor
SF
Sourci
(l1l8I SIC )
9.591-02
O.OOE+OO
6.22E-02
4.38E-03
1.m-01
6.10£-02
0.00£+00
o.ooe+oo
2.63E-03
0.001+00
Carbon Tltrachloride
ACltone
1,1-Dichlorlthene
1,2'DichlorOithene
TetrlchlorOithene
T I' i clll orOithene
Methylene Chloride
Vinyl Chloride
1,1 DichlorOlthlnl
Carbon Disulfide
Totlls
Carbon Tetrachloride
ACltone
1,1'Dichlorethene
1,2-DlchlorOithene
TltreehlorOithene
TriclllorOltll..
Mlthyl.. Chloride
Vinyl Chloride
1,10lchlorOlthlnl
Carbon Disulfide
Totals
~PPENCIX ~
PAGE 9 OF 9
IJr;tten:
Author:
Printed:
08-Jan-91
OCPalmer/ICKerrigan
08-Jan-91
,~
AII' Cone Intlkl
(l1li.-3) (l1li/ k;! day)
2.m-03 3.04e-oa 3.95E-Q9
O.OOE+OO O.OOE+OO O.OOE+OO
1.76E-03 1.97E-oa 2.36E-oa
1.24E-04 1.39£-09 O.OOE+OO
3.461-03 3.87E'08 6.96E-11
1.90e'03 2.12E-oa 3.61E-10
O.OOE+OO O.OOE+OO O.OOE+OO
0.00£+00 O.OOE+OO O.OOE+OO
7.44£-05 8.32E-10 O.OOE+OO
0.00£+00 0.00£+00 O.OOE+OO
2.80E-08
Risk
AII' Conc Intakl
(../.-3) (../kg/day)
2.m-03 2.13e.06 3.04E'04
O.OOE+OO O.OOE+OO O.OOE+OO
1.76E-03 1.381-06 1.531'04
1.241-04 9.71E-oa 4.85!-01
3.461-03 2.71E-Q6 2.71E-05
1.90e-03 1.48E-06 ERR
0.001+00 o.ooe+oo O.OOE+OO
O.OOE+OO O.OOE+OO ERR
7.44£~05 5.aze-oa 5.82£-08
O.OOE+OO O.OOE+OO O.OOE+OO
4.84E'04
Ca)W:lchronlc Ol'll RfO util ized lIher. S&8tIl'onic Imilition 1ft not IVlillblt.
(b)lnhllation value fro. IRIS.
Cc)lnhllation value fro. "EAST, 4th OuIrttr, FY 1990.
Cd)Orll value fro. IRIS.
(t)Orll value fro. MEAST, 4th Quarter, FY 1990.
Cf)Subchronic value not avallablt; chronic value utilized.
Cg)VIlue not aVlillbte on IRIS.
Risk
Subchronic VllUlS not available on IRIS.
Sourct . Liquid Concentrltion . FlOll Rltt . Littrs per gallon I seconds per mi~te
Air concentration. sourct . CX/G)
Int.kt . CAir concentration. IR . ET . EF . ED) / (BW . AT>
Risk Cfor cancer) . Intlkt . Slope Factor
------- |