UNITED STATES
ENVIRONMENTAL PROTECTION AGENCY
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PRELIMINARY EVALUATION REPORT
WATER POLLUTION CONTROL FACILITY
NEW HOLLAND, PENNSYLVANIA
CONTRACT NO. 68-03-2223
Gannett Fleming Corddry and Carpenter, Inc.
Engineers
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Harrisburg, Pennsylvania
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UNITED STATES
ENVIRONMENTAL PROTECTION AGENCY
PRELIMINARY EVALUATION REPORT
WATER POLLUTION CONTROL FACILITIES
NEW HOLLAND, PENNSYLVANIA
CONTRACT NO. 68-03-2223
GANNETT FLEMING CORDDRY AND CARPENTER, INC.
ENGINEERS
HARRISBURG PENNSYLVANIA
U.S. EPA Region III
Regional Center for Environmental
Information
1650 Arch Street (3PM52)
Hiiiadslphia, PA 19103
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TABLE OF CONTENTS
Page
SUMMARY iii
INTRODUCTION 1
DESCRIPTION OF FACILITY 2
TREATMENT PLANT EVALUATION 6
General Performance 6
Process Performance 14
OPERATION AND MAINTENANCE 20
ADMINISTRATION 24
CONCLUSIONS AND RECOMMENDATIONS 27
APPENDICES 29
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SUMMARY
A preliminary evaluation was conducted at a 1.0 mgd trickling
filter treatment plant owned by the New Holland Borough Authority. Ad-
ministrative procedures at the plant were found to be satisfactory. The
treatment plant currently employs two full-time operators. Employment
of an additional operator for maintenance purposes is recommended.
Three areas of operation were identified as needing some im-
provement or modification. The recommendations include:
1. Initiate a primitive maintenance schedule to
eliminate equipment breakdowns.
2. Institute proper housekeeping procedures to
achieve a cleaner and better functioning plant.
3. Authorize the preparation of an operation and
maintenance manual for the plant.
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INTRODUCTION
This report sets forth the findings and recommendations
from a preliminary evaluation of a biological wastewater treatment
facility at New Holland, Pennsylvania. The evaluation was conducted
under the U. S. Environmental Protection Agency (EPA) Contract No.
68-03-2223 by Gannett Fleming Corddry and Carpenter, Inc. , Harrisburg,
Pennsylvania. The New Holland plant is one of a number of biological
wastewater treatment plants being studied under this contract. It is
anticipated that this sampling of treatment facilities will help to
identify operational and maintenance program improvements which will
enable the performance of some treatment plants to be upgraded with
minimal capital expenditures.
The evaluation program discussed in this report consisted of
field inspection, discussions with supervisory and administrative per-
sonnel, process sampling and analysis, and collection of past operating
and performance data. Operational procedures and problems encountered in
the past were discussed with the treatment plant staff. Treatment efficiency
during the study was evaluated from grab samples of influent, effluent,
and intermediate flows collected daily. Past performance was assessed
by analysis of one year's operating records supplied by the plant super-
intendent. Administrative, staffing, and budgetary information were also
obtained during this preliminary evaluation.
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DESCRIPTION OF FACILITY
New Holland is located approximately 15 miles northeast of
Lancaster, Pennsylvania. The Borough's wastewater treatment plant
presently provides sanitary sewage services for a population of 4000.
In addition to domestic wastewater, approximately 10 percent of the
total flow to the plant is industrial wastewater. Cheese processing
and paint manufacturing represent the major industries served by the
treatment facility.
Constructed in 1940, the original plant consisted of primary
clarification, trickling filtration, secondary clarification, and
chlorination. Additional primary and secondary clarifiers, and a sludge
digester were added in 1959. The plant has been designed to accommodate
an average flow of 1.0 mgd. Separate stormwater and sewage collection
systems are provided at New Holland.
Infiltration/inflow problems with the sewage system have been
experienced in the past; however, repairs to the system to correct the
problems are gradually being made.
Treated effluent from the New Holland plant is discharged to
Mill Creek. Mill Creek is a tributary of Conestoga Creek which, in turn,
is a tributary of the Susquehanna River. The National Pollutant Discharge
Elimination System (NPDES) permit program sets forth the various effluent
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requirements for the New Holland plant for discharging to Mill Creek.
These requirements are divided into interim and final limitations. In-
terim requirements are in effect until July 1, 1977, and final require-
ments are to be met after that date. The permit requirements are as
follows:
Interim
Parameter
bod5
suspended solids
Fecal coliform
pH
50-day requirement
30 rag/1
30 mg/1
200 colonies/100 ml
6.0 to 9.0
7-day requirement
45 mg/1
45 mg/1
400 colonies/100 ml
6.0 to 9.0
Final
bod5
suspended solids
Fecal coliform
pH
Ammonia-Nitrogen
P04 as P
Dissolved oxygen
6 mg/1
25 mg/1
200 colonies/100 ml
6.0 to 9.0
2.0 mg/1
2.0 mg/1
5.0 mg/1
6 mg/1
25 mg/1
400 colonies/100 ml
6.0 to 9.0
2.0 mg/1
2.0 mg/1
5.0 mg/1
Additional effluent requirements for the plant are provided under
a permit issued by the Pennsylvania Department of Environmental Resources
(DER). The requirements under this permit, however, either parallel or
are less stringent than those set forth by the NPDES.
DER has established water quality criteria for the section of
Mill Creek at the point of discharge. The principal uses of the stream
include water supplies for domestic and industrial concerns, water-contact
recreation, irrigation and propagation of wildlife, fish, and other aquatic
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life including cold-water fishes. In addition, the region has been
designated as a conservation area.
The New Holland facility utilizes the trickling filtration
process to accomplish secondary treatment. Ferric chloride and polymer
are initially added to the influent wastewater for increased primary
solids removal. Two barminutors then each receive half of the flow.
Following preliminary treatment, the wastewater enters the primary
sedimentation stage, consisting of two rectangular settling tanks and
one circular clarifier. The effluent from the primary stage is then
biologically treated by two high-rate trickling filters. Following
the biological step, final settling is provided by one circular clarifier.
Disinfection occurs in the chlorine contact tanks, which comprise both
the original rectangular settling tanks and the original chlorine
contact tanks. The final effluent is discharged to Mill Creek. Settled
sludge is anaerobically digested and hauled to nearby farms for disposal.
Design characteristics for the individual unit processes within the
facility are summarised in Appendix A. Figure I provides a process flow
schematic of the facility.
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WASTEWATER TREATMENT FACILITIES
NEW HOLLAND, PA.
RETURN SLUDGE
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TREATMENT PLANT EVALUATION
General Performance
The New Holland treatment facility was evaluated to determine
whether its performance conforms with the design intent and permit require-
ments. Data regarding performance were compiled from three sources. The
first, EPA Form 7500-5, "Report on Operation and Maintenance of Wastewater
Treatment Plant," was completed during the field investigations conducted
by Gannett Fleming Corddry and Carpenter, Inc. personnel. This document
is presented herein as Appendix B. The available operating records maintained
by treatment plant personnel served as a second source. This information as
well as important operational parameters, is set forth in Appendix C. The
final source included a sampling and analysis program of the influent and
effluent wastewater flows and characteristics for each major plant unit
process. This program was the major activity during a three-day field
study conducted at the plant as part of the preliminary evaluation. The
results of the survey sampling and analysis program are shown in Table I.
Table II presents a summary comparison of recent operating records, survey
data, design parameters, and permit requirements.
As indicated in Table II, wastewater parameters such as flow,
BODt^settleable solids, suspended solids, fecal coliform, chlorine residual,
and pH are monitored regularly at the New Holland plant. From January 1976
through December 1976, the average daily wastewater flow was 0.645 million
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TABLE I
Preliminary Evaluation Survey Analytical Results
Wastewater Treatment Facility
New Holland, Pennsylvania
Influent Wastewater
Flow (mgd)
BOD5 (rag/1)
Suspended Solids (mg/'l)
Volatile Suspended Solids (mg/1)
Settleable Solids (ml/1)
Dissolved Oxygen (mg/1)
pH
Temperature (°C)
Original Primary Effluent
BOD5 (mg/1)
Suspended Solids (mg/1)
Settleable Solids (ml/1)
PH
New Primary Effluent
BOD5 (mg/1)
Suspended Solids (mg/1)
Settleable Solids (ml/1)
PH
Trickling Filter Effluent
Dissolved Oxygen (mg/1)
pH
Final Clarifier Effluent
BOD5 (mg/1)
Suspended Solids (mg/1)
Volatile Suspended Solids (mg/1)
Final Effluent
BOD5 (mg/1)
Suspended Solids (mg/1)
Volatile Suspended Solids (mg/1)
Settleable Solids (ml/1)
Dissolved Oxygen (mg/1)
pH
Chlorine Residual
2/8/77
0.799
1018
484
452
15
4.9
7.8
11
814
472
27
6.7
641
264
Trace
6.8
5.1
7.3
540
196
184
552
200
186
0.1
5.5
6.8
0.2
2/9/77
0.728
600
15
5.7
7.3
10
464
18
7.2
204
0.1
6.9
2.9
7.3
196
174
Trace
5.1
7.1
0.1
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TABLE I (Cont'd)
2/8/77
2/9/77
Primary Clarifier Sludge
Suspended Solids (mg/1)
Volatile Suspended Solids
Secondary Clarifier Sludge
Suspended Solids (mg/1)
(ng/l)
40,000
35,800
1,060
Liquid Digested Sludge
Suspended Solids (mg/1) " 42,900'
Volatile Suspended Solids (mg/1) 34,000
Digester Supernatent
Alkalinity (mg/1)
B0D5 (mg/1)
Suspended Solids (mg/1)
Volatile Suspended Solids (mg/1)
Settleable Solids (ml/1) 5
Volatile Acids
pH 5.9
920
2,741
550
500
3,500
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tabu: i 1
A COMPARISON 01-' OPERATING PERFORMANCE, DI.SIGN INTENT, AND EFFLUENT REQU1REMENTS
WASTEWATER TREATMENT l-AC11.1TY
NEW HOLLAND, PENNSYLVANIA
F LOW (mgd)
Domestic
]ndustrial
Total
SETI l.EABLE SOLIDS (ml/I)
Influent
Effluent
Percent Removal
SUSPENDED SOLIDS (mg/1)
Influent
Effluent
Percent Removal
5-DAY BOD (ml/I)
Influent
Effluent
Percent Removal
Plant Operating
Records
Average
0.580
0.065
0.645
10.1)
0.2
97
228
23
89
263
38
84
Peak
] .720
50.0
0.6
99
856
102
99
619
66
97
Preliminary Plant
Evaluation Data
Average
0.688
0.076
0.764
15.0
0.1
99
54 2
186
66
1,018
548
54
Peak
0.799
15.0
0.1
99
600
192
70
578
Design
Average
1.00
Peak
220
33
85
220
33
85
NPDES Effluent
Ueqin rements
30-day 7-day
Average Average
25
25
COD
Influent
Effluent
Percent Removal
AMMONIA NITROGEN (as N)
Influent
Eff1uent
Percent Removal
2.0
2.0
TOTAL PHOSPHORUS (as P)
Influent
Effluent
Percent Removal
2.0
2.0
DISSOLVED OXYGEN (mg/1)
Effluent 6.2
FECAL COLI FORM (No./100 ml)
Effluent 6.4
CHLORINE RESIDUAL 0.6
11.5
2,400
1.0
5.3
0
0. I
5.5
0
0.15
Minimum
5.0
200
M inimum
5.0
400
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gallons. Influent BOD^ and suspended solids concentrations for the
same period were 263 mg/1 and 228 mg/1, respectively. The final
effluent BOD5 concentration was reported to average 38 mg/1, and
the suspended solids concentration, 23 mg/1. BOD^ and suspended
solids removals of 84 percent and 89 percent respectively, were
obtained. Throughout the 12-month period, the chlorine residual
was maintained at an average 0.6 mg/1, while effluent fecal coliform
counts averaged 6.4 colonies/100 ml. It should be noted that plant
personnel indicated that problems were experienced with the chlorina-
tion equipment during the past severe winter. This resulted in devia-
tions from the reported average coliform count.
A comprehensive sampling program was performed during the
preliminary evaluation. However, the data obtained were the result
of a three-day study and may not be representative of average conditions
on a long-term basis. Columns 3 and 4 of Table I summarize the major
operating parameters investigated. Presented together with the influent
and effluent data are sampling data for the individual unit processes
and the intermediate stream. Sampling points included the primary
clarifier effluent, trickling filter effluent, and final clarifier
effluent. Analyses conducted on samples from the major process streams
included temperature, BOD5, suspended solids, volatile solids, settleable
solids, pH, and dissolved oxygen. The various sludge handling process
streams were also evaluated. Specifically, primary sludge, secondary
sludge and digester contents were examined for volatile and suspended
solids. Digester supernatent was analyzed for BOD5 and volatile suspended
and suspended solids.
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The results of the three-day sampling program indicated
that during that period the plant was not in conformance with the
NPDES effluent limitations. However, it was noted that at the time
of the study the plant was experiencing problems resulting from
what were believed to be wastes from a local cheese processing
industry. This industrial waste caused extremely high influent
BOD5 and suspended solids concentrations. The BOD5 concentration
was 2.8 times the normal level, while the suspended solids concen-
tration was 1.4 times the previous year's average. BOD5 and suspended
solids removal for the preliminary study period differed substantially
from the year's operating data, probably as a result of the sudden
overload condition. Removal for the study period averaged 54 percent
and 66 percent respectively. For the previous year's operating data,
similar averages were 84% and 89%. Effluent dissolved oxygen concentrations
during the evaluation averaged 5.3 mg/1. In order to compare the plant
effluent quality with NPDES requirements, 7-day and 50-day average con-
centrations were computed using actual plant operating data. This infor-
mation, presented in Table III, indicates that the maximum 7-day average
BOD5 and suspended solids concentrations were 66 mg/1 and 102 mg/1,
respectively, exceeding the respective interim permit limitations 30
percent and 14 percent of the time. Similarly, the maximum 30-day
average BOD5 and suspended solids concentrations were found to be
66 mg/1 and 49 mg/1, respectively, while the limitations as defined by
secondary treatment were exceeded 92 percent and 50% of the time. The
7-day and 50-day average performance parameters are summarized in Table IV.
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MILL
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
GPERATING REPCRT 01/01/76 - 12/31/76
7 DAY AMD 30 DAY AVERAGES
7 DAY
AVERAGES
AVERAGES
WASTEWATER
FINAL EFF
FINAL EFF
FINAL EFF
fecal
MASTEWATER
FINAL EFF
FINAL EFF
FINAL EFF
FECAL
DATE OF
FLOW
D.O.
8C0(5 DAY)
SUS SOLIDS
CCLIFORM
DATE UF
FlQw
0.0.
60D< 5 DAY)
SUS SOLIDS
COLI FORM
1. AST DAY
(M GO )
(MG/L)
(MG/L)
(fG/LI
(ORG./lOO)
LAST DAY
( M GO )
C MG/L)
0.6714
5.233
25.CC
18.33
1 .000
8-25-76
0.6643
5.725
2E.00
14. 75
1 .000
8-27-76
0.6737
5.742
37.OC
1 9. 07
2. 332
9- 1-76
0.6571
6.020
IE. CC
10. 75
1 98.0
9- 8-76
0.6086
6 0 C 0
O.C
11.50
1 .000
9-15-76
0.6229
5. 76C
12.00
8. 800
190.0
9-22-76
0.7829
4. 600
36.CC
12. 00
0. 0
9-26-76
0o5 4 3
5.923
33. 33
9. 923
33.51
9-29-76
0.6143
6 .000
52. OC
15. 00
2d.00
10- 6-7o
0.7460
5.65C
26. CC
15.75
0. 0
10-13-76
0.7043
6.050
28.00
12.40
1 .000
\
10-20-76
0 66 86
7.150
53.OC
15.00
0.0
10-26-7t>
0.6954
6. 136
34.25
13. 94
4. 982
10-27-76
0.70 14
5.825
3C.CC
14.00
2 2.00
11- 3-76
0.6529
6.267
54. 00
16. 33
I .000
11-10-76
0.6500
5.967
3S. CC
20. 25
5.000
1 1-17-76
0.5986
7.5CC
C.C
20. 00
1 .000
11-24-76
0.6686
7.750
43. CO
26. 00
15.00
1 l-25-7o
0.6425
6.410
45. 33
2C. 67
2.371
12- 1-76
0.6071
0.0
C.C
0.0
0. 0
12- 8-7o
0.7300
0.0
O.C
O.O
0.0
12-15-76
0.6771
6 . 400
C.C
46. OC
10. 82
12-22-76
C.6543
6.867
66.CO
31 . 00
1 .000
12-25- /6
0.6737
6.680
66. OC
37. 00
4. 691
12-29-76
0.6357
6.733
C.C
32 . 67
63. 00
12-3 1-76
0. /7u0
7.100
47. CC
24 . CO
0. 0
12-31-76
0 .6920
6.925
4 7. 00
30. 50
63 . 00
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TABLE IV
7- AND 30-CONSECUTIVE-DAY
AVERAGE PERFORMANCE SUMMARY
WASTEWATER TREATMENT FACILITY
NEW HOLLAND, PENNSYLVANIA
7-CONSECUTIVE-DAY AVERAGE CONCENTRATION
Suspended
Solids
BODc
Fecal Coliform
Maximum Value
102 mg/1
66 mg/1
198/100 ml
Number of Times
Permit Limitation
Exceeded
10
Percent of Time
Permit Limitation
Exceeded
14
30
30-CONSECUTIVE-DAY AVERAGE CONCENTRATION
Maximum Value
Number of Times
Permit Limitation
Exceeded
Percent of Time
Permit Limitation
Exceeded
Suspended
Solids
49 mg/1
6
50
BODi;
66 mg/1
11
92
Fecal Coliform
33/100 ml
0
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Process Performance
For a thorough evaluation of the treatment performance,
the operational efficiency of key unit processes within the plant
must be examined. In this section, therefore, the analytical data
and design parameters compiled for these processes are compared
with corresponding data for properly designed and operated facilities.
For comparison, sources of reference include the EPA process design
manual for "Upgrading Existing Wastewater Treatment Plant," and
various wastewater treatment texts.
The original primary settling tanks at the New Holland plant
were designed to accommodate an overflow rate of 1,100 gallons per day
per square foot (gpd/ft^) at an average influent flow of 1.0 mgd. The
*7
new primary clarifier was designed for an overflow rate of 700 gpd/ft"
at the same 1.0-mgd flow. These figures assume an equal distribution
of flow between the old and new clarifiers. At these surface loading
rates, detention times are approximately 2.5 hours for the original
settling tanks and 2 hours for the new clarifier. As indicated, the
average flow to the facility is currently 0.65 mgd. Therefore, the
present actual overflow rates are 460 gpd/ft^ f°r the new, and 720 gpd/ft^
for the old clarifiers. Actual detention times are 3.1 hours for the
new, and 4.0 hours for the old clarifiers. The EPA process design
literature recommends that overflow rates range from 800 to 1200 gpd/ft^.
During the three-day study, raw waste BOD5 and suspended solids
concentration averaged 1,018 mg/1 and 542 mg/1, respectively. BOD5 and
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suspended solids concentration in the new primary clarifier effluent
were approximately 641 mg/1 and 234 mg/1. Similarly, BOD5 and suspended
solids concentrations for the original primary clarifier effluent were
814 mg/1 and 468 mg/1, respectively. Therefore, the respective BOD^
and suspended solids primary removal efficiencies were 37 percent and
57 percent for the new clarifier, while the old primary clarifier removal
efficiencies were 20 percent and 14 percent for the same pollutants.
The effluent settleable solids removal efficiency for the new primary
clafirifer averaged 99 percent. Effluent settleable solids concentra-
tions for the original primary clarifier were higher than those of the
raw waste. Plant operating records do not indicate the unbalanced primary
clarifier performance shown during the survey. According to operating
records, the new primary clarifier averaged an 82 percent removal of
settleable solids, and the original primary settling tanks, an 89 percent
removal.
The secondary treatment stage of the New Holland plant consists
of biofiltration and final clarification. The trickling filters were
designed to accommodate hydraulic and organic loads of 5.0 mgd/acre and
19.5 lb BOD5/IOOO ft-Vday, respectively. An examination of the operating
data shows that hydraulic and organic loads averaged 3.07 mgd/acre,
excluding recirculation, and 17.4 lb BOD^/iOOO ft3/day, respectively.
Because primaiy effluent BOD5 data were not available, a reduction of 25
percent in the raw waste BOD5 load through the primary clarifiers was
assumed for calculating the organic load on the biological system. In
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addition, the recirculation ratio for the same period was determined
to be 0.7. The EPA process design manual recommends that high-rate
trickling filters provide for hydraulic loads of 10 to 30 mgd/acre and
organic loads of 30 to 60 lb BOD5/IOOO ft-Vday. Including recirculation,
hydraulic loads of 5.2 mgd/acre are experienced at New Holland. There-
fore, the design of the trickling filters would be classified as con-
servative.
The final clarifier at New Holland was designed to provide
approximately 1.9 hours of detention time at 1.4 mgd (0.7 recirculation
ratio). Final clarifier overflow rates currently average 330 gpd/ft^.
The design overflow rate is 560 gpd/ft^, including recirculation. The
EPA process design manual suggests that overflow rates for secondary
clarifiers following trickling filters range from 400 to 600 gpd/ft^.
A review of the three-day evaluation data indicates that the final
clarifier effluent suspended solids concentrations averaged 196 mg/1,
an obviously excessive concentration. However, this was under the
previously described condition of extremely high load due to industrial
wastes. Under normal operating conditions, secondary clarifier effluent
is not monitored, so unit performance is unknown. However, the process
load and design figures would indicate that any performance problems
in secondary clarification during normal loading would be a result
of poor sludge characteristics, rather than clarifier design.
The chlorination facilities at the New Holland plant were
examined with regard to design and performance. At an average flow of
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1.0 mgd, the chlorine contact tanks provide approximately 20 minutes,
detention. The chlorine residual is usually maintained at about 0.6 rag/1,
although during the three-day study a 0.1-mg/l residual was reported.
At present flows, secondary effluent undergoes a 23-minute contact time
prior to final discharge. The "Recommended Standards for Sewage Works-
Great Lakes-Upper Mississippi River Board of Sanitary Engineer," commonly
referred to as the Ten-State Standards, suggests a contact time of at
least 15 minutes during peak flow periods. Chlorine residuals commonly
range from 0.2 to 0.5 mg/1 in properly operated facilities. Inasmuch
as the fecal coliform analyses indicated that no colonies were present
in the evaluation study samples, and the average fecal coliform count during
the 12-month period prior to the evaluation was 6.4 cells per 100 ml, it
appears that disinfection facilities at the New Holland plant are adequate
and are performing satisfactorily.
According to plant operating records, the primary clarifiers,
both old and new, are not performing adequately. Although settleable
solids analysis is the only one regularly performed on primary effluent,
indications are that the percent removals are not sufficient. Settleable
solids should be almost completely removed, allowing only suspended matter
to pass into the primary effluent. The additional settleable solids place
an increased burden on the trickling filters and final clarifier.
During the three-day study, settleable and suspended solids
analyses were performed on both primary effluents. As indicated, the
new primary clarifier far exceeded the performance of the old primary
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clarifiers, a condition which was apparently related to the unusually
high influent pollutant concentrations observed. The inordinately high
suspended solids loads were due, according to the plant personnel, to
effluent from a cheese processing plant. Although the cheese processing
plant has pretreatment facilities, New Holland personnel believed that
those facilities were not operating properly at the time of the high
BOD^ and suspended solids loads in the plant. This had been documented
by the plant's consulting engineer. Unequal loads on the primary clarifiers
caused by blockages of their respective bar screens may have caused the
unbalanced performance of the new primary clarifier in relation to the
old.
At the time of the study, both barminutors were observed to be
inoperative and awaiting parts for repairs. During such times the bypass
bar screens must be manually cleaned several times per day. Failure to
do so results in clogging of the bar screens and an extremely unbalanced
flow distribution to the clarifiers. Such an unbalance can overload one
clarifier, causing high solids carry-over for that unit. Poor primary
clarification will naturally interfere with the efficiency of the trickling
filters.
The sludge treatment facilities at the New Holland plant were also
evaluated. Sludge from the primary clarifiers is pumped directly to the
anaerobic digester. Sludge from the secondary clarifier is returned to
the head of the plant and settled in the primary clarifier. After digestion
in the unheated digester, sludge is trucked as a liquid to nearby farms.
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A mass balance study was performed to compare the pounds
of solids removed from the wastewater with that removed from the
digester. For the recorded 12-month period, an average 2,720 gallons
per day were hauled from the digester, at an average concentration of
39,900 mg/1. Thus, for the year, the average rate of removal of solids
from the digester was 910 lbs/day. The average influent suspended
solids concentration was 228 mg/1, which is equivalent to a daily
influent suspended solids load of 1,230 pounds. Effluent suspended
solids concentrations averaged 23 mg/1 for the same period. Thus,
solids leaving the plant in the effluent amounted to approximately
120 lbs/day. Net solids removal through treatment averaged 1,010 ihs/day.
This value is reasonably close to the above solids removal rate from
the digester of 910 lbs/day.
The above analysis also compares well with published data.
For example, according to EPA figures, approximately 1,500 pounds of
solids are typically generated per million gallons of wastewater treated
in a plant such as New Holland. Therefore, under average flow conditions,
(approximately (0.645) at New Holland, one would expect about 1,000 lbs/day
of solids to be produced for disposal.
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OPERATION AND MAINTENANCE
During the three-day study, various characteristics of
the facility operation and maintenance were evaluated. Table V
presents a summary evaluation of plant performance indicators at
New Holland. As shown, the overall operation of the plant is adequate,
though some areas of maintenance are marginally adequate or inadequate.
In general, many items of equipment are worn excessively, are old, or
are obsolete. This is due, in part, to the original plant being almost
40 years old.
There is no preventive maintenance program at the plant.
iMaintenance intervals for the equipment are excessively long, and
treatment reliability due to equipment downtime is inadequate. Various
pieces of equipment including both barminutors, were inoperative at the
time of the survey. This necessitates the frequent manual cleaning of
the bar screens. If left unattended, as during weekend operation, the
blocked screens cause improper flow proportioning to the primary clari-
fiers. Another equipment malfunction noted was the inoperative distributor
arm on one of the trickling filters. According to plant personnel, this
arm periodically ceases operation and causes poor bacterial growth on
the rock media. Under such a condition, the performance of the trickling
filter is inadequate.
Plant housekeeping was also less than adequate. The control
room, office, and work room appeared excessively cluttered. It appears
-20-
-------
TAHI,I: V
EVALUATION OP VARIOUS OPERATION AND MAINTENANCE PHRl-OliMANCIi INDICATORS
wastewater treatment facility
NEW HOLLAND, PENNSYLVANIA
PLANT UBORATORY
Hqui pment
Condition
Analytical Capabilities
Orgaiu zation
Records
Sampling Procedures
OPERATION MANUAL
Quality and Completeness
Operating Procedures
Equipment Information
Use and Understanding by Operators
CONTROL PROCEDURES AND RECORDS OP UNIT PROCESSES
Understanding of Process Fundamentals
Degree of Process Control Exercised
Interpretation and Understanding of Process
Response to Control Adjustments
Records
Adequate
Marginally
Adequate
Inadequate
Nonexislent
MAINTENANCE PROVISIONS AND PROCEDURE,S
Routine
Maintenance Intervals for all Equipment
Spare Parts Inventory
Treatment Reliability (absence of downtime)
"Mousekeeping" Procedures
Emergency
Availability of Backup Units
Parts Accessibility and Procurement
Records of Repairs and Corrective Maintenance
Alann Systems for Power or Equipment Failure
ADEQUACY OF STAFFING AND SHIFT COVERAGE
Operation
Ma intenance
Laboratory
-------
that there is no system for the storage of equipment, and as a result,
equipment is left lying around haphazardly.
No emergency maintenance program has been established at New
Holland. Although backup equipment, such as portable pumps, generators
and spare chlorinators, are not available for use throughout the plant,
emergency units and most parts are readily accessible. Also, major units
and equipment, except secondary clarifiers, have been provided in parallel
configuration, allowing one unit to handle the entire hydraulic load tempor-
arily, if necessary, during maintenance or repair. In general, emergencies
are handled satisfactorily at New Holland. Records of repairs and corrective
maintenance are filed at the plant and appear satisfactory.
The laboratory at the New Holland plant contains the necessary
equipment for performing the analysis required under the NPDES permit and
the process control testing. Analyses of primary clarifier effluent settleable
solids and pH are normally conducted twice weekly. Also analyzed twice weekly
is the trickling filter effluent dissolved oxygen. Percent total and volatile
solids and pH tests are analyzed from samples of wet sludge when it is
pumped from the digester. Effluent BOD^ determinations are performed on
final clarifier samples, and all other effluent parameters, on the chlorine
contact tank effluent samples. Records of laboratory analyses appear complete
and copies are filed and maintained systematically.
The personnel operated and maintain the facility without the aid
of an operations manual. The lack of a complete reference manual has apparently
-22-
-------
not had deleterious effect on the management of the facility.
Although process control is an important factor in the operation
of any biological plant, a biofiltration plant is less amenable to such
control than are the suspended growth systems. Nevertheless, the plant
personnel are familiar with biological process fundamentals, and they apply
these principles where applicable at New Holland. The staff is capable
of identifying and developing solutions to process upsets as they occur
within the system. In addition, the staff has demonstrated the ability
to determine the system's response to various control measures.
-23-
-------
ADMINISTRATION
Operations at the New Holland facility are conducted during
one shift, 8 hours daily, 5 days weekly. One- to two-hour inspections
are made on weekends for pumping operations and routine maintenance. A
superintendent, plant operator, and laborer make up the three man staff.
Section E of Appendix B presents the estimated labor efforts devoted to the
various work areas within the operation of the facility. These estimates
represent the actual manpower expenditures as determined through inter-
views with the plant superintendent.
For comparison, a study of staffing requirements was performed
in accordance with the EPA publication "Estimating Staffing for Municipal
Wastewater Treatment Facilities." Appendix F sets forth the results of this
investigation. As shown, approximately 3.6 persons should be employed to
operate and maintain the treatment facility properly. This estimate
indicates that the staff size at the facility is deficient by approximately
one person. The areas where a need for more manpower is indicated include
operation and maintenance. In both of these categories, the present manpower
is approximately one-half the amount recommended. All other categories com-
pare favorably with the recommended level of effort. As previously discussed,
certain areas of operation and maintenance were found to be in need of
improvement. It would appear that an additional person should be employed
at the treatment facility. Because the areas of concern require qualified
personnel, it would be recommended that any new employee be certified by
-2d-
-------
the State of Pennsylvania to insure proper operation of the New Holland
plant.
The operating budget for the New Holland treatment facility is
summarized in Table VI. Total expenses for the year 1976, were approxi-
mately $48,000. Based on the average annual influent flow of 0.645 mgd,
the total cost of treatment is approximately 20.4
-------
TABLE VI
ANNUAL BUDGET
WASTEWATER TREATMENT FACILITIES
NEW HOLLAND, PENNSYLVANIA
Salaries and Wages $ 10,700
Maintenance and Repairs
Machinery and Equipment $ 6,800
Contracted Supplies 800
Subtotal $ 7,600
Supplies
Materials $ 6,900
Gas, Grease and Oil 1,700
Major and Minor
Equipment Replacement 1,800
Subtotal $ 10,400
Fuel and Electric $ 4,100
Chemicals $ 10,600
Contracted Services $ 1,500
Sludge Hauling $ 3,100
Total $ 48,000
-------
CONCLUSIONS AND RECOMMENDATIONS
The results of the preliminary evaluation presented in this
report indicate that the New Holland wastewater treatment facility is
not producing an acceptable effluent and is not consistently meeting
regulatory agency permit requirements. Generally, the treatment problems
observed at the plant are a result of inadequate maintenance, excessive
age of certain items of equipment, and process upset due to equipment
failure.
While operational procedures at the plant are adequate, maintenance
procedures for many equipment items must be improved. For example, at the
time of the survey, the barminutors, trickling filter bearings, and chlorinators
were operating improperly and were in need of repair. Poor performance of the
plant is attributed by plant personnel, to food processing wastes from local
industries, resulting in fluctuating and unreasonable loads. However, analysis
of operating data and design parameters indicate that the facility has the
capacity to assimilate the wastes it normally receives. If all equipment
were properly maintained, and full use of the plant thereby allowed, the
occasional shock loads could be better controlled. To allow for improved
maintenance programs, an increase in the operating staff size appears
necessary. As stated, the EPA staffing estimate indicates that at least one
more person should be employed at the treatment plant. According to that
estimate, this person is most critically needed in operation and maintenance.
-27-
-------
Analysis of budgetaiy information indicates that funds currently
allotted for operation and maintenance of the facility are adequate. In
addition to the recommendations discussed, several specific improvements
are needed in the operation of the treatment facility. The New Holland plant
is currently operated and maintained without the aid of an operations manual.
Although the plant performance currently appears to be unaffected by this
deficiency, a complete manual should be kept at the facility. Such a
reference may prove useful in readily solving future problems at the plant
as well as in training future personnel. It should be prepared by a
consulting engineering or a similarly qualified firm retained by the Borough
of New Holland. As a further improvement, ferric chloride and polymer should
be added to the influent waste stream only when necessary, rather than con-
tinuously. This would decrease operating costs and reduce the amount of
operator attention needed to attend to this system.
-28-
-------
APPENDICES
-------
APPENDIX A
-------
APPLNI) 1 X A
GliNLKAl, DESCRIPTION 01-' SliWAGC TRP.ATMLNT PLANT UNIT HkOCliSSLS
WASTCWATP.K TKI-ATMLNT FACILITY
NI".W 1101,1.AND, PENNSYLVANIA
Process Component
Preliminary Treatment
Flow Measurement
Screening
Comminution
Grease or Oi 1
Flotation
Overflow or Bypass
Fac illty
Grit Removal
Type of Unit
Parshall flume
In-line cumininutor
Dimensions (ft)
Number of SWD
Units Diameter Length Width Depth
Rema rks
9" thioat
1. Unit bypasses for pr imary ,cla r i f i e is, trickling filters,
and secondary clarifier
Primary Treatment
Primary
Sediinentat ion
Other
Secondary Treatment
lliologica]
Unit Process
Aeration Equipment
Sedimentation
Bas ins
Ois infection
Chlorir.ators
Chlorine Contact
Tank
New primary clarifier 1
Old settling tanks 2
Trickling filter
Final clarifier
Gas
30
76'4"
50
30
20
7'6" 1'. Total volume = 39,650 gal; detention time = 1.9 hrs @
1.0 mgd; overflow rate =707 gpd/tt- @ 1.0 mgd; weir
loading = 5,330 gpd/ft
7.5 7'9" 3. Total volume = 13,000 gal ea; detention tune = 2.5 hrs @
1.0 mgd; overflow rate = 1,1 10 gpd/ft^; weir loading -
33,300 gpd/ft
7.0 4. Surface area = 4,570 ft2; hydraulic loading = 4.76 mgd/
acre @ 1 mgd; BOD loading = 19.5 lb/1,000 ft"' @ 1 mgd,
150 mg/1
7.9 5. Total volume = 116,000 gal; detention tjine = 2.7 hrs
-------
APPENDIX B
-------
ENVIRONMENTAL PROTECTION AGENCY
DATE OF INSPECTION
REPORT ON OPERATION AND MAINTENANCE
OF WASTEWATER TREATMENT PLANT
h~orrn Approved
OMSfVr. I'jS-ROQ^
A. GENERAL INFORMATION
1 . PLANT
(a.) NAME
New Holland 3. T. D.
(b.) OWN ER
New Holland Borousn Authontv
(c.) LOCATION
New Holland. Pennsylvania
2. TYPE Or PLANT
High-rate trickling filter
3. PROJ ECT NO.
4. AVG. DESIGN FLOW (mfZU)
1.0 mgd
S. DESIGN POPULATION
EQUI VAL ENT
4500
5. COLLECTION SYSTEM
7. DATE °R ES EN T PLANT 6EG AN OPERATING
1959
8. STATE PERMI 7 NO.
0021890
[combined j X [separate
] 3 O TH
9. IN THE SPACE PROVIDED BELOW, FURNISH A SIMPLIFIED FLOW DIAGRAM OR A WRITTEN DESCRIPTION OF THE PLANT UNITS IN
FLOW SEQUENCE.
10. IDENTIFY RECEIVING l.VA7E°S
Mill Creek
11. IDENTIFY = ERT'NENT -STREAM STANDARDS AND OP USES OF THE RECEIVING WATERS
Propagation of warm water fish, water supplies, fishing, water contact recreation, power, and
treated waste assimilation
12. GIVE T ^ E EFFLUENT STANDARDS AND.OR REQUIREMENTS FOR STATE OPERATING PERM IT
See page 2
B. CURRENT PLANT LOADING
1. annual AVG DAILY FLOW RATE (mtfcO
0.645
2. PEAK FLOW 0 A T E (m«d)
DRV -VEATHE= J WET WEATHER
3. POPULATION SERVED
4500
4. AN N U AL AVG 30 D 5 OF RAW S EW A G E (mg/l)
265
5. ANNUAL AVG SUSPENDED SOLID OF RAW SEWAGE (mg/l)
223
6. PRINCIPAL TY3 ES OF INDUSTRIAL WASTE DISCHARGED TO
MUNICIPAL SYSTEM
Cheese processing and paint manufacturing (infrequent)
7. POPULATION EQUIVALENT (BOO) OF INDUSTRIAL WASTES
N/A
3. POPULATION EQUIVALENT ($S) OF INDUSTRIAL WASTES
N/A.
9. VOLUME OF INDUSTRIAL WASTES (ri&ti)
0.10
10. INFILTRATION PROBLEMS
Infiltration/inflow problems immediately following heavy precipitation
EPA Form 7500-5 (4-72) REPLACES FORM FVrPCA - 12 WHICn IS OBSOLETE.
-------
Harm Approved
OMB No. 15S-R00i5
C PLAN T PERFORMANCE
1.
LABORATORY ANALYSIS (Total Plant)
(a) REPORTING PERIOD
FROM (Month, year)
TO (Month, veer)
MONTHLY ITEMS
(b)
ACTUAL PLANT
PERFORMANC E
DATA
(e)
PLANT
DESIGN
DATA
(d>
NPDES
PERMIT
REQUI REMENTS
PLANT
ACHIEVES
DESIGN
EFFICIENCY
m
Pi. At
COMPL
WITH PE
REQUIRE
fe
iT
1 ES
RMIT
MENTS
(O
YES
NO
v es
NO
(1)
FLOW (mgd)
(monthly average)
0.645
1.0
X
(2)
PEAK FLOW (mgd)
(maximum day)
1.72
2.5
(3)
SETTLEASLE SOLIDS
(monthlv average)
INFLUENT (ml/ 1)
10.9
EFFLUENT (ml/1)
0.2
T. REMOV AL
97°s
U)
SUSPENDED SOLIDS
(monthly average)
IN FLUES T (mg/ I)
228
200
. EFFLUENT (mg/ 1)
25
50
30
X
X
7. REMOVAL
39
85
--
(5)
900^ (monthly average)
INFLUENT (mg/ 1)
263
200
EFFLUENT (mg/ 1)
58
50
50
X
X
% REMOVAL
34
35
(5)
DISSOLVED OXYGEN
(monthly average)
EFFLUEN T (mg/ I)
6.2
(7)
CHLORINE RESICUAL
(monthly average)
EFFLUENT (mg/ 1)
0.6
(9)
COLI FORM (per 100 ml)
(monthly average)
TOTAL
F EC AL
6
200
X
(9)
pH RANGE EFFLUENT
MINIMUM
3.5
6.0
X
MAXIMUM
3.1
9.0
X
(10)
TOTAL PHOSPHORUS (asP)
(monthly average)
IN FLUENT (mg/ I)
EFFLUEN T (mg/ 1)
1
r. P E MOV AL
(11)
TOTAL NITROGEN (as i\)
(monthly average)
influen " (mg/1)
EFFLUENT (mg/1)
1
r. REMOVAL
2. PLANT RECORDS
ARE MONTHLY OPERATING RECORDS FILED WITH ST^TE AGENCY' [Yj \ES 1 j NO
EPA Form 75 00-5 (R«v. 1-74) FAGS 2 replaces page 2U-72) ivhich is obsolete
-------
Form Approved
OMB No. 158-RQ035
3. DOES PLANT HAVE ALTERNATE ELECTRIC POWER SOURCE'
| | 0UAL FEED Q GENERATOR fj3 NONE
4. ADEQUATE ALARM SYSTEM FOR POWER OR EQUIPMENT
FAILURES' 2JVES ~ NO
5.
EQUIPMENT PROGRAM
(a.) ROUTINE MAINTENANCE SCHEDULES
(b.) RECORDS OF MAINTEN AN C E.REP AIRS & REP L CM T
(c.) £°ASE PARTS INVENTORY
ADEQUATE
I N A D E QU A T £
X
5. IS PLANT EFFLUENT
BEING CHLORINATED?
IXJ VES ~ NO
7. DOES SEWAGE 0Y-PASS
PLANT IN WET WEATHER
1 | Y ES [X] NO
3. DOES SEWAGE 9Y-PASS
PLANT IN DRY
WEATHER'
j ) Y ES NO
9. AGENCIES NOTIFIED OF EACH 0Y PASS
N/A
10. BYPASS FREQUENCE
(Mo nth I v)
No
1 1. AVG DURATION OF
BYPASS (Mrs)
12. REASON FOR BYPASSING
13. CAN BYPASS SEWAGE BE
CHLORINATED? Qyes Q no
14. DO SEWER OVERFLOWS OCCUR
UPSTREAM OF PLANT'
I I YES
CS N0
15. ANY ODOR COMPLAINTS BEYOND °LAN T PROPERTY? (If yes, explain)
No
16. OBSERVED APPEARANCE OF EFFLUENT, RECEIVING STREAM OR DRAINAGE WAY
Turbid with light brown solids
17. IS A CONSULTING ENGINEER RETAINED OR AVAILABLE FOR CONSULTATION ON OPERATING AND MAINTENANCE PROBLEMS'
IX j YES | | NO (If yes, check one of Che following) | I CONTINUING BASES I j REQUEST BASES
18. DO 0° ERA TORS AND OTHER PERSONNEL ROUTINELY ATTEND SHORT
COURSES. SCHOOL OR OTHER TRAINING' [XJ yes Q] NO
(a.) yes, cite course sponsor, and date of last course.
Course offered by Public Service Inst, and the Pennsylvania
State University
(b.) It no. 3re there any courses available m this area3
(c.) Is there an established procedure tor tratning new operators3
19. IS LAB TESTING ADEQUATE C0R THE CONTROL
REQUIRED FOR THIS SIZE AND TYPE OF PLANT
AND USES OF RECEIVING WATERS'
|~X Y ES rn NO (If No, explain)
20. EXPLAIN MAIN DIFFICULTY EXPERIENCED WITH INDUSTRIAL WASTES
Very high suspended solids and BOD5. Whey waste doesn't settle well and as a result, much of it passes
through the plant. The waste reportedly retards growth of the biological film on the trickling filters and
also overloads the digester.
2'. PERMANENT RECORD FILE
(a.) PLANT OPERATION AND MAINTENANCE MANUAL' ~ YES Q NO (b.) AS BUILT PLANS AND SPECIFICATIONS' Kj VES [j Mt
Cc.) MANUFACTURERSOPERATION & MAINTENANCE SPECIFICATIONS' [j YES Q no (d.) FLOW CHARTS' [Jyes P] NO
22. ESTIMATED WEEKLY MAN-HOURS FOR LAB WORK INCLUDING MAINTENANCE OF RECORDS AND PREPARATION OF REPORTS
10 hours/week
23. ANNUAL 3UDGET FOR MAINTAINING AND OPERATING PLANT
SALARIES & WAGES ELECTRICITY CHEMICALS MAINTENANCE STAFFING i TRAINING OTHER
10,700
4,100
10,600
7,600
15,000
48,000
24. STABILIZATION PONDS
(a.) WEEDS CUT AND VEGETATION GROWTH IN PONDS REMOVED'
1 I Y ES | I NO
(b.) BANKS AND DIKES MAINTAINED' (Erosion, etc.;
I I Y ES I I NO
(c.) ANY REPORTS OF GROUND WATER CONTAMINATION FROM POND' (It yes, Hive aerails) ~ Y ES |j NO
(a.) SEE = AGE REPORT
~ Y ES fj NO
(e.) ADEQUATE OEDTH CONTROL'
n YES | | NO
(f.) EFFLUENT RELEASE IS
CONTINUOUS I i INTERMITTENT
SEASON AL
EPa Form 7500.5 (4-72) PAGE 3
-------
Form Approved
OWB No. 15S-R0035
d. laboratory control
CODING INSTRUCTION
Enter test codes opposite appropriate items. If any or the below tests are used to monitor industrial wastes, place an "X" in
addition to the test code.
1 - 7 or more per week 3-1, 2 or 3 per week 5 - 2 or 3 per month 7 Quarterly 9 - Annually
2-4, 5 or 6 per week 4 - as required 6-1 per month 8 - Serru-Annually
ITEM
(a.)
RAW
(b.)
PRIMARY
EFFLUENT
(c.)
MIXED
LIQUOR
(d.)
FINAL
(e.)
(f.) SLUDGE
DIGESTER
(g.)
RECEIVING
STREAM
(h.)
RAW
SUPER.
NATANT
1. BOD
3
3
2. SUSPENDED SOLIDS
3
3
3. SETTLE40LE SOLIDS
2
2
2
4. SUSPENDED VOLATILE
3. DISSOL V ED O X Y G EN
3
6. TO T AL SOLI DS
3
7. VOLATILE SOLIDS
3
8. pH
2
2
3
9. T EMP ERATURE
10. CO LIFORM DENSITY
3
It. RESIDUAL CHLORINE
2
1 2. VOL ATIL E ACIDS
13. MB STABILITY
M. ALKALINITY
\ 5.
1 .
I 7.
1 8.
19.
COMMENTS
-
E. PLANT PER50NNEL INVENTORY
PERSONNEL CLASSIFICATION
(a.)
EMPLOYMENT
(b.)
(c.) CERTIFICATION
training Required
NEXT 12 MONTHS
(d.)
VO L UN T A R Y
M AND ATORY
ACTUAL
NUMBER
BUDGETED
NO. RE-
COMMENDED
NO. RECOM-
MENDED OR
R EQUI RED
BY STATE
ACTUAL
NO.
CERTIFIED
NEW
HIRES
UPGRADE
(JVomorton
or skill /m-
provement
M AN-HOU RS
PER WEEK
NUMBER
1. MANAGEMENT/SUPERVISOR
10
0.25
0.25
0.3
1
2. OP ERATOR
33
0,875
0.375
1.6
1
3. L A BO R A TO R Y
10
0.25
0.25
o :
to
4. MAINT EN A N C E
25
0.625
0.625
1.2
5. OTHER PLANT WORKERS
20
0.5
0.5
0.3
6. OTHER OFFICE/CLERICAL
7- total
100
2.5
2.5
3.6
2
EPA Form 7SOO-5 (4-72) PAGE 4
-------
Form Approved
OMK No. 158-R0035
| F. GUIDE - VISUAL OBSERVATION - UNIT PROCESS
j RATING CODES: S = Satisfactory; U = Unsatisfactory; M = Marginal, IN - In Operation, OUT = Out of Operation
CONDITION OR APPEARANCE
RATIN G
COMMEN TS
GENERAL
G RO UN DS
S
9UIL Dl NGS
U
Poor condition
SQTA0LE WATER SUPPLY P SO T
s
SArETY F E A TURES
M
Minimal equipment
9YP ASSES
S
STORM WATER OVERFLOWS
S
MAINTENANCE OF COLLECTION SYSTEMS
PUMP STATION
>
C
<
z
2
VENTIL ATION
BAR SCREEN
IN
At times not cleaned often enough
DISPOSAL OF SCREENINGS
S
COMMINU TOR
OUT
Out of order
X
Q.
GRIT CHAMBER
DISPOSAL OF GRIT
PRIMARY
SETTLING TANKS
IN
Insufficient solids removal
SCUM R EMO V AL
S
SLUDGE REMOVAL
s
E F FLU EN T
M
High solids carry over
SLU DGE DISPOSAL
DIGESTERS
IN
TEMPERATURE AND OH
M
Disester not heated, poor digestion in winter
GASP RO DU CTICN
M
HEATING EQUIPMENT
SLUDGE PUMPS
IN
DRYING BEDS
VACUUM Fl L T E R
INCINERATION
DISPOSAL OF SLUDGE
S
OTHER
FLOWMETER AND RECORDER
IN
RECORDS
S
LAB CONTROLS
S
> -S
<¦ c
H =
X 5
w
1- V
i I
< 5
Q ~
z
O '
u ^
A
!
1
CHLORINE
EF^LUEN T
M
Effluent turbid
CHLOR1NATORS
IN
One chlormator out of service
EFFECTIVE OOSAGE
S
CONTACT TIME
S
CONTACT TANK
IN 1
EPA Form 7500-5 (4-72) PAGE 5
-------
/ onn Apprnnct/
OMtt Vo. 153-KQOlj
G NOTATIONS BY ^VALUATOR
1. OPERATION AND MAINTENANCE P ROB L E MS/0 E F I CI E NC I ES
CHECK EACH CP THE FOLLOWING ITEMS IN TERMS Or THEIR ESTIMATED ADVERSE iFFECT ON THE PERFORMANCE OF THE PLANl
STAFF COMPLEMENT
OVERLOADS
-------
APPENDIX C
-------
M'tT.NDf X C
NE In HOLLAND. PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
04/06/7 T
PAGE I OF 9
PART 1 OF 6
DATE
WASTEWATER
FLOW
(MOD)
RAW WASTE
600(5 DAYI
(MG/LI
RAW WASTE
SUS SOLIDS
(MG/L)
RAW WASTE
SET SOL I OS
IML/L)
RAW WASTE
PH
(UNIT S I
NEW PRI EF
SET SOLIDS
(ML/LI
7
P.C. REM.
SET SOLIDS
NEW P CLAR
NF. W PRIM.
EFF. PH
(UNIrsi
1-
1-
1-
1-
1-
1-
1-
1-76
2-76
3-76
4-76
5-76
6-76
7-76
1- 8-76
1- 9-76
1-10-76
1-11-76
1-12-76
1-13-76
1-14-76
1-15-76
1-16-76
1-17-76
1-18-76
1-19-76
1-20-76
1-2 1-76
1-22-76
1-23-76
1-24-76
1-25-76
1-2 6-76
1-27-76
1-23-76
i-29-76
1-30-76
1-31-76
2- 1-76
2- 2-76
2- 3-76
2- 4-76
2- 5-76
2- 6-76
2- 7-76
2- 8-76
2- 9-76
2-10-76
2-11-76
2-12-76
2-13-76
2-14-76
0.6800
0.6900
0.7200
0.5700
0.6900
0.7000
0.6600
0.7100
0.6700
0.5000
0.5600
0.7200
0.8 200
0.6800
0.6800
0.7100
0.5400
0.5600
1.7 10
1.720
0.6700
0.7200
0.6800
0.5700
0.5700
0.t>500
1 .080
0.6200
0.5600
0.6800
0.3300
0.5700
0.5600
0.5400
0.6000
0.3700
0.6100
0.3900
0.3300
0.5000
0.52C0
0.4800
0.5100
0.5200
0.3500
116.C
218. C
126.0
211.0
242. C
19 6.0
238.0
258. C
235. C
241.0
2C2.0
197.0
6. 000
10.00
4. 000
12.00
9. 500
10.00
12.00
7.500
10.00
4.000
9.000
5.000
7. 000
12 .00
7.800
7. 500
7.300
7.500
7.700
7.500
7. 600
7 .600
7 . 500
7.600
7.300
7 . 500
7. 100
7.600
0.9000
0.3000
0.0
0.2000
0.2000
1.200
0.5000
0.7000
0.3000
0.2000
0.2000
0.3000
0 .3000
0.2000
85. CO
97. CO
98.33
97. 89
88. CC
95.83
90.67
97.CO
95.on
97.78
94. 00
95.71
98.33
r. 700
7. 400
7.300
7. 600
7.600
7.300
7.400
7.500
7.400
7. 500
7.200
7.4 00
7. 300
7.400
-------
NEW HOLLAND, PA WASTtWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 2 OF 9
PA k T 1 OF 6
04/06/77
1
2
3
4
5
6
7
8
WASTEWATER
RAW WASTE
RAW WASTE
RAW WASTE
RAW WASTE
NEW PR 1 EF
P.C. REM.
NEW PR
FLUW
BOO(5 DAY 1
SUS SOL I OS
SET SOLIDS
PH
SET SOLIDS
SET SOLIDS
EFF. 1
DAT E
(MGD>
(MG/L)
(MG/L)
( fL/L )
(UNITS)
(ML/L)
NEW P CLAR
( UNI T
2-15-76
0.3200
_
_
_
.
.
2-16-76
0.48 00
-
-
9.000
7.100
0 . 2000
97. 78
7.200
2-17-76
0.5300
-
247,0
-
-
-
-
-
2-1 8-76
0.49 00
-
-
12 .00
7. 500
0.0 T
-
7. 100
2-19-76
0.4800
-
-
10.00
7.300
0. 1000
99.00
7. 300
2-20-76
0.47 00
-
-
-
-
-
-
-
2-21-76
0.3900
-
-
-
-
-
-
-
2-22-76
0.3400
-
-
-
-
-
-
-
2-23-76
0.4900
240. C
-
7.000
7. 100
0. 1000
98.57
7. 200
2-24-76
0.5000
-
-
19.00
7.000
0.3000
98. 42
7.400
2-25-76
0.4700
-
-
-
-
-
-
-
2-26-76
0.4200
-
-
-
-
-
-
-
2-2 7-76
0.4400
-
-
12.00
7.600
0.2000
98.33
7.400
2-28-76
0.4100
-
-
-
-
-
-
-
2-29-76
0.4300
-
-
-
-
-
-
-
3- 1-76
0.5600
-
-
2.000
T.500
-
-
7. 300
3- 2-76
0.5900
-
-
12.00
7.200
0.9000
92.50
7.400
3- 3-76
0.6000
-
-
-
-
-
-
-
3- <.-76
0.7800
-
-
5. 000
7.000
0.7000
86.CO
7. 000
3- 3-76
0.7800
-
-
-
-
-
-
-
3- 6-76
0.5400
-
-
-
-
-
-
-
3- 7-76
0.5000
-
-
-
-
-
-
-
3- 8-76
0.6800
-
-
-
-
-
-
-
3- 9-76
0.6800
-
-
7.000
7. 500
-
-
-
3-10-76
0.6000
-
-
10.00
7.400
-
-
-
3-11-76
0.7300
-
-
-
-
-
-
-
3-12-76
0.6900
-
-
-
-
-
-
-
3-13-76
0.6300
-
-
19.00
7.100
0.2000
98. 95
7.200
3-14-76
0.4300
-
¦
-
-
-
-
-
3-15-76
0.6800
-
-
-
-
-
-
-
3-L6-76
0.6800
-
-
-
-
-
-
-
3-17-76
0.6400
-
-
-
-
-
-
-
3-18-76
0.6700
-
-
5. 000
7.300
0.2000
96.00
7.500
3-19-76
0.6300
-
-
-
-
-
-
3-20-76
0.5500
-
-
-
-
-
-
-
3-21-76
0.5000
-
-
-
-
-
-
-
3-22-76
0.7400
-
-
-
-
-
-
-
3-23-76
0.6100
-
184.0'
7.000
a .000
0.3000
95.71
e. 700
3-24-76
0.6600
-
-
0.000
7.600
0.2000
97.50
7.500
3-25-76
0.6100
-
-
-
-
-
-
-
3-26-76
0.6500
258* C
-
-
-
-
-
-
3-27-76
0.5900
-
-
-
-
-
-
-
3-28-76
0.5100
-
-
-
-
-
-
-
3-29-76
0.7400
-
-
12.00
7.300
0.3000
97. 50
7.400
3-30-76
0.6600
-
-
-
-
-
-
-
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT
OPERATING REPOR1 01/01/76 - 12/31/76
DATA TABLE
PAGE 3 OF 9
PAPT 1 OF 6
04/06/77
DATE
WAS!EwATfcR
FLOW
(MGD)
RAn WASTE
BOO(5 DAY)
(HG/LI
RAW WASTE
SLS SOLIDS
(MG/l »
RAW WASTE
SET SOLIDS
(ML/LI
RAW WASTE
PH
(UNITS I
NEW PR I EF
SET SOLIDS
(ML/L)
7
P-C. REM.
SET SOLIDS
NEW P CLAR
NEl" PRIM.
(IFF. PH
( UNI TS)
3-31-76
4- 1-76
4- 2-76
4- 3-76
4- 4-76
4- 5-76
4- 6-76
4- 7-76
4- 6-76
4- 9-76
4-10-76
4-11-76
4-12-76
4-13-76
4-14-76
4-15-76
416-76
4-17-76
4-18-76
4-19-76
4-20-76
4-21-76
4-22-76
4-23-76
4-24-76
4-25-76
4-2 6-76
4-27-76
4-2 8-76
4-29-76
4-30-76
5- 1-76
5- 2-76
5- 3-76
5- 4-76
5- 5-76
5- 6-76
5- 7-76
5- 8-76
5- 9-76
5-10-76
5-11-76
5-12-76
5-13-76
5-14-76
0.e900
0.5900
0.6700
0.5600
0.5500
0.7200
0.7100
0.6800
0.7000
0.7000
0.6000
0.5300
0.6900
0.6900
0.6600
0.6900
0.5800
0.5900
0.4900
0.7200
0.7100
0.6400
0.6900
0.6300
0.5300
0.5200
0.6600
0.6700
0.6300
0.6900
0.6700
0.6200
0.5000
0.7000
0.6700
0.6600
0.6700
0.6200
0.5100
0.5300
0.7100
0.7200
0.7200
0.6200
0.6 5 00
197.C
247.C
232.C
159. C
101. C
310. C
23C. C
204.0
178.0
168.0
2C9.0
176.0
188.0
15.00
20.00
10.00
7.000
13.00
8. 000
21.00
28.00
16.00
7.000
11.00
9.000
10.00
15.00
159.0
7.000
7.500
7.800
7.400
7.600
7.500
T. 300
7. 500
7.300
7 .900
7. 100
7. 300
7.000
7. 300
7. 100
7. 300
7. 300
0.3000
0.9000
1.000
0 .8000
3. 500
4.000
7.000
1 .600
0.9000
0.9000
0.3000
0.2000
0.3000
0.3000
98.00
S5. 50
90.00
ea.57
73.08
50.OC
6 6.67
94.29
94.38
87. 14
97.27
97.78
97.00
98.CO
1. 300
7. 500
7.900
7. 300
7. 800
7.600
7.400
7.500
7. 500
7.200
7.400
7.200
7.600
7.200
7.400
F 'I' v !"> t r\
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA T ABLE
PAGE 4 OF 9
PART 1 OF 6
04/06/77
DATE
1
WASTEWATER
FLO H
( MGD I
RAW WASTE
BOD< 5 DAY)
(MG/L)
RAW WASTE
SUS SOLIDS
(fG/L)
RAW WASTE
SET SOLIDS
(ML/LJ
RAW WAST t
PH
(UNITS)
NEW PRI EF
SET SOLIDS
(ML/LI
7
P.C. REM.
SET SOLIDS
NEW P CLAk
NEW PRIM.
EFF. PH
(UNITSl
5-15-76
5-16-76
5-17-76
5-18-76
5-19-76
5-20-76
5-21-76
5-22-76
5-23-76
5-24-76
5-25-76
5-26-76
5-2 7-76
5-28-76
5-29-76
5-30-76
5-31-76
6- 1-76
6- 2-76
6- 3-76
6 476
6- 5-76
6- 6-76
6- 7-76
6- 8-76
6- 9-76
6-10- 16
6-11-76
6-12-76
6-13-76
6-14-76
6-15-76
6-16-76
6-17-76
6-18-76
6-19-76
6-20-76
6-21-76
6-22-76
6-23-76
6-24-76
6-25-76
6-26-76
6-27-76
6-28-76
0.5500
0.5500
0.7300
0.6900
0.6700
0.7000
0.6300
0.5300
0.5000
0.6900
0.7600
0.6800
0.6100
0.5900
0.5100
0.4400
0.4600
0.7400
0.6700
0.6900
0.6200
0.5600
0.4600
0.6200
0.6500
0.6200
0.6200
0.7300
0.5800
0.5200
0.7 100
0.7400
0.7600
0.7600
0.7000
0.5200
0.5500
0.7700
0.7200
0.6500
0.7100
0.5800
0.5100
0.4800
0.7600
475. C
256.0
21 .00
10.00
147. C
175.C
103.0
250.0
13.00
9.000
143.C
486. C
241.0
186.0
7. 000
171.0
121. C
7. 200
7.400
7.600
7.400
7.500
7. 100
7.300
7.800
7.000
7. 300
7. 500
7.300
7 .200
7.400
7.700
7. 100
7.400
7. 100
0.6000
0.5000
97. 14
95.OC
0.8000
0.6000
93.85
93.33
0.6000
91.43
7.400
7. 200
7. 200
7.200
7. 100
7. 300
7. 100
7.200
7.400
7.300
7.300
7. 300
7.4 00
7. 000
7.300
7. 200
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 5 OF 9
PART 1 OF 6
04/06/77
12345678
WASTEWATER RAW WASTE RAW MSTE RAW WASTE RAH WASTE NEW PR I EF P.C. FF.M. NEW PRIM.
FLOW 80D< 5 DA YI SUS SOLIDS SET SOLIDS PH SET SOLIDS SET SOLIDS EFF. PH
DATE (MGD) IMG/LI (NG/L» (ML/L) (UNITS) (ML/LJ NEW P CLAP (UNITS)
6-2 9-76
6-30-76
7- 1-76
7- 2-76
7- 3-76
7- 4-76
7- 5-76
7- 6-76
7- 7-76
7- 8-76
7- 9-76
7-10-76
7-11-76
7-12-76
7-13-76
7-14-76
7-15-76
7-16-76
7-17-76
7-18-76
7-19-76
7-20-76
7-21-76
7-22-76
7-2 3-76
7-24-76
7-2 5-76
7-26-76
7-2 7-76
7-28-76
7-29-76
7-30-76
7-31-76
8- 1-76
8- 2-76
8- 3-76
8- 4-76
8- 5-76
8- 6-76
8- 7-76
8- 8-76
8- 9-76
8-10-76
6-11-76
8-12-76
0.7 300
0.6700
0.7100
0.6400
0.5300
0.4200
0.5600
0.7800
0.7900
0.7 200
0.7100
0.6600
0.5000
0.7700
0.7000
0.7000
0.7000
0.7100
0.5800
0.5100
0.7100
0.Y500
0.7400
0.6200
0.7 300
0.5800
0.5400
0.7 200
0.7000
0.7000
0.8100
0.6100
0.4500
0.4100
0.7100
0.7700
0.5900
0.7200
0.7900
0.6900
0.6200
0.7700
0.7800
0.7100
0.7500
222.C
187.0
7.400
7.700
7. 400
7. 300
212.C
491.C
178. C
150. C
178.0
152.0
100.0
8 5 6.0
406. 0
100.0
96. 00
103.0
105.0
143.0
7.000
10.00
12.00
18 .00
10.00
6.000
9.000
3.000
13.00
17.00
15.00
50.00
1 0.00
8.000
7.500
10.00
10.00
8.000
6.000
8.000
8.000
10.00
6.300
6. 500
6.900
6. 800
6.800
r.ooo
6.900
6.700
200
900
800
700
200
6.400
7.200
7.400
7. 500
7. 300
7.000
7.600
7.400
7. 500
20.00
15.00
0.9000
10 .00
10.00
1.500
0.9000
0.7000
8.000
6.000
5.000
3. 500
3.000
5.000
1.500
3.500
2.500
3.500
4.000
7.000
5. 500
5.500
-185.7
- 50.00
92. 5C
44.44
0.0
75. OC
90.00
76.67
38.46
64.71
66.67
93.00
70.00
37.50
80.00
65.00
75.00
56.25
33.33
12.50
31.25
45.00
6. 200
6. 600
6.800
6. 700
6. 500
6.700
6. 900
6. 500
6.300
6. 500
6.700
6. 600
6. 800
6. 800
7. 000
7.200
6.900
7,2 00
6. 900
7.200
6. 900
6. 400
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLAN1
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 6 OF 9
PART I OF 6
04/06/7 7
DATE
WAST fcWATER
FLOW
(MOD)
RAW WASTE
BCIDI 5 DAY I
(MG/L(
RAW WASTE
SOS SOLIDS
(MG/L)
RAW WASTE
SET SOLIDS
(ML/L)
R AW W AS T E
PH
(UNITS)
NEW PR I EF
SET SOLIDS
(ML/L )
P.C. REM.
SET SOLIDS
NEW P CLAR
NEW PRIM.
EFF. PH
( L'NI T S )
8-13-76
8-14-76
8-15-76
8-16-76
8-17-76
8-18-76
8-19-76
8-20-76
8-21-76
8-22-76
8-23-76
8-24- 16
8-25-76
8-26-76
8-27-76
8 2 8-76
8-29-76
8-30-76
8-31-7b
9- 1-76
9- 2-76
9- 3-76
9- 4-76
9- 5-76
9- 6-76
9- 7-76
9- 8-76
9- 9-76
9-10-76
9-11-76
9-12-76
9-13-76
9-14-76
9-15-76
9-16-76
9-17-76
9-18-76
9-19-76
9-20-76
9-21-76
9-22-76
9-23-76
9-24-76
9-25-76
9-26-76
0.7100
0.5 5 00
0.5400
0.74 00
0.6300
0.78C0
0.6900
0.7400
0.5300
0.5100
0.8200
0.6500
0.7100
0.7 300
0.7000
0.5100
0.5100
0.7600
0.7100
0.6800
0.6800
0.7000
0.4800
04600
0.5300
0.7300
0.6b00
0.7000
0.6900
0.5000
0.5400
0.7300
0.5200
0.6800
1 .280
0.76 00
0.5500
0.4700
0.8 200
0.7700
0.6JOO
0.7200
0.6800
0.4900
0.4700
159. 0
279.0
91.OC
394. C
161. C
280. C
88. 00
186.0
186.0
2fa0.0
122.0
162.0
124.0
205.0
182.0
14C.0
296.0
167.0
132.0
102.0
180.0
102.0
106.0
178.0
162.0
6.000
13.00
12.00
14.00
7.000
9.000
8.000
10.00
9.000
12.00
6.000
10.50
9.000
7.500
8.000
8. 500
500
500
000
8.000
7.000
5.500
7.400
7.200
7.300
700
500
200
7.400
7. 500
7. 200
7.400
7.300
7.300
7. 300
7. 300
7. 100
7. 200
7. 200
7. 700
7.000
3.500
2.500
2.000
5.000
2.500
2.500
3. 500
2.000
1.400
1.000
0.9000
1.500
0.5000
1.000
1 .000
1. IOC
0.5000
1.000
0.4000
0.7000
0.4000
41.67
80. 77
83. 33
64.29
64. 2 9
72.22
56.25
86.00
88.89
92.50
75.CO
95.24
88. 89
06.67
86.25
94. 12
89.47
94.67
91.25
95.00
6. 500
6. 400
5.900
6.700
6.800
7. COO
6. 800
6. 900
6.500
6. 000
6.400
6. 900
6.600
6. 500
7.000
6. 800
6.700
7.000
7.000
7. 100
6. 900
332. C
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 1.2/31/76
DATA TA8LE
PAGE 7 OF 9
PART 1 OF b
04/06/77
DATE
1
WAS r EW AT ER
FLOW
I MGO )
RAW WASTE
BOD(5 DAY)
(MG/L)
RAW WASTE
SUS SOLIDS
C MG/L)
RAW WASTE
SET SOLIDS
< fL/L)
RAW WASTE
PH
IUN1TS)
NEW PRI EF
SET SOLIDS
CML/LI
P.C. REM.
SE T SOI ID S
NEW P CLAR
NEK PRIM.
EFF. PH
IUNI1SI
9-27-76
9-28-76
9-29-76
9-30-76
10- 1-76
10- 2-76
10- 3-76
10- 4-76
10- 5-76
10- 6-76
10- 7-76
10- 8-76
10- 9-76
10-10-76
10-11-76
10-12-76
10-13-76
10-14-76
10-15-76
10-16-76
10-17-76
10-18-76
10-19-76
10-20-76
10-21-76
10-22-76
10-23-76
10-24-76
10-25-76
10-26-76
10-27-76
10-28-76
10-29-76
10-30-76
10-31-76
- 1-76
- 2-76
- 3-76
- 4-76
- 5-76
- 6-76
- 7-76
- 8-76
- 9-76
-10-76
0.7100
0.6200
0.6100
0.7800
0.7800
0.7&00
0.7300
0.6800
0.7300
0.7700
0.7400
0.5900
0.7500
0.7200
0.6300
0.6700
0.6 8 00
0.5100
0.4500
0.6900
0.7100
0.9700
0.7700
0.6700
0.5500
0.6000
0.7600
0.£400
0.7200
0.6600
0.7000
0.5700
0.5700
0.7 4 00
0.6700
0.6400
0.6900
0.6700
0.6800
0.6100
06000
209. C
381. 0
357. C
496.0
293.0
106.0
224.0
220.0
262.0
262.0
278.0
194.0
274.0
240.0
352.0
190.0
236.0
250.0
380.0
220.0
278.0
308.0
51 0.0
350.0
206.0
222.0
9.500
16.00
15.00
11 .00
10.00
17.00
11.00
12.00
8.500
9.000
9. 000
8. 500
15.00
10.00
20.00
8.000
10.00
6. 000
10.00
10.00
9. 500
7. 500
11.00
11.00
9. 000
13.CO
700
700
600
7. 700
500
900
7. 500
7.600
7.600
7. 200
7. 300
7.600
7. 500
7.800
7.600
7. 400
7.900
7.400
1.500
1.300
1.300
1.000
1.900
1.200
0.8000
1.200
0.5000
1.500
2.000
0.4000
1.400
1.600
0.6000
0.5000
1.300
0.7000
2.000
0.9000
0.7000
0.4000
0.4000
1.000
1.500
1.600
84. 21
<51.88
SI. 33
SO.<31
81 .00
92. 94
92. 73
90.00
94. 12
03.33
77.78
9 5.29
90.67
84. CO
97.00
93. 75
87.CC
88.33
80.00
91.CO
92.63
94.67
96. 36
90.91
83. 33
e7.69
7. 100
7. 000
7. 100
8.300
7. 3 00
7. 700
6. COO
7. 000
7. 300
7.400
7. 000
7. 500
7. 300
7.600
6. 900
7.200
7.'.00
7. 500
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT PAGE 8 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 1 OF 6
DATA TABLE
04/06/77
DATE
WASTEWATER
FLOW
(MGD )
RAW WASTE
BOD< 5 DAY)
(MG/LI
RAW WASTE
SUS SOLIDS
(MG/LI
RAW WASTE
SET SOLIDS
(fl/Lt
RAW WASTE
PH
(UN ITS I
b
NEW PRI EF
SET SOLIDS
(ML/LI
7
P.C. REM.
SET SOLIDS
NEW P CLAR
NEW PRIM.
EFF. PH
(UNITS)
11-11-76
11-12-76
11-13-76
11-14-76
11-15-76
11-16-76
11-17-76
11-18-76
11-19-76
11-20-76
11-21-76
11-22-76
11-2 3-76
11-24-76
11-25-76
11-2 6-76
11-27-76
11-28-76
11-29-76
11-30-76
12- 1-76
12- 2-76
12- 3-76
12- 4-76
12- 5-76
12- 6-76
12- 7-76
12- 8-76
12- 9-76
12-10-76
12-11-76
12-12-76
12-13-76
12-14-76
12-15-76
12-16-7b
12-17-76
12-18-76
12-19-76
12-20-76
12-2 1-76
12-22-76
12-23-76
12-24-76
12-25-76
0.6400
0.5900
0.4900
0.5000
0.6300
0.6900
0.6500
0.6800
0.7100
0.6000
0.5300
0.7200
0.6800
0.7600
0.5800
0.5800
0.5900
0.5300
0.7000
0.6200
0.6500
0.6900
0.6700
0.9900
0.7600
0.7900
0.8600
0.7000
0.7200
0.7300
0.5800
0.6100
0.7100
0.7100
0.6800
0.6700
0.7700
0.5300
0.5200
0.7100
0.7100
0.6700
0.6500
0.6500
0.4600
360.0
370.0
374.0
454.0
296.0
20 7.0
3fe6.0
380.0
27C.0
13 .00
13.00
16.00
11.00
13.00
1J .00
18.00
8.000
14.00
15.00
9. 000
8.000
8.500
7.800
7.500
8.000
7.600
8.500
7.600
8 .200
7.800
7.700
7.800
7.300
7.600
7. 400
0.4000
0.5000
0.3000
0.4000
0.3000
1.000
0.4000
0.7000
0.7000
0.7000
1.000
0.3000
0.0
96.92
96.15
98. 13
96. 36
97.69
90. 91
97.78
91.25
95.00
95. 33
88.89
96.25
7. 500
7.400
7. 500
7. 500
7.400
7.300
7.400
7. 600
7.400
7. 300
7. 400
7. 100
7.200
428.0
-------
NEW HOLLANO > PA WASTEWATER TREATMENT PLANT PAGF 9 OF 1
OPERATING REPORT 01/01/76 - 12/31/76 PART 1 OF 6
DATA TABLE
04/06/77
DATE
WAi TEwATER
FLOW
IMGD)
RAW WASTE
BOD(5 DAY)
IMG/L)
RAW WASTE
SIS SOLIDS
(MG/L)
RAW WASTE
SET SOLIDS
(PL/L)
RAW WAS I E
PH
(UNITS)
NEW PRI EF
SET SOLIDS
(ML/LI
P.C. REM.
SET SOLIDS
NEW P CLAR
NEW PRIM,
t F F . PH
( UN!T SI
12-26-76 0.6600
12-27-76 0.7000 1 - 324.0 15.00 8.000 1.100 92.67 7.000
12-28-76 0.6800 - 166.0 12.00 7.500 1.000 91.67 7.000
12-29-76 0.6500 - 246.0 13.00 7.700 OilOOO 99.23 7.100
12-30-76 0.7700 619.C 216.0 15.00 7.900 0.5000 96.67 7.000
12-31-76
MINIMUM
MAX I MUM
AV ERAGE
ST 0.DEV.
VLD.PTS.
0.3200
1.720
0.64 53
0.1397
361
91.00
619.0
263.-4
126. 3
39
88.00
856.0
22e.4
111.0
86
2.000
50.00
10.90
5.248
134
5.500
8 . 800
7.380
0.3943
145
0.0
20.00
1.745
2.739
132
-ies.7
99.23
81. J8
32.27
128
5. 900
8.700
7.158
0.3901
1 39
NOTE - ( ) SEE FOOTNOTE TABLE.
* SEE COMMENT TAbLE.
T.G.L. OR 0 = TRACE. GREATER THAN. LESS THAN, OR QUESTIONABLE DATA.
-------
NtW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 1 OF 9
PART 2 OH 6
04/06/77
DATE
OLD PR I EF
SET SOLIDS
(ML/L )
1C
P .C. REM.
SET SOLIDS
OLD P CLAR
11
OLD PRIM.
EFP . PH
(UNITS)
12
FILTER EFF
PH
(UMTS I
13
FINAL EFF
SET SOLIDS
C ML/L)
14
PC OVERALL
SET SOLIDS
REMOVED
15
F INAL
EFFLUENT
PH (UNITS)
16
TRICK F1LT
EFF 0.0.
(MG/L)
1- 1-76
1- 2-76
1- 3-76
1- 4-76
1- 5-76
1- 6-76
1- 7-76
1- 8-76
1- 9-76
1-10-76
1-11-76
1-12-76
1-13-76
1-14-76
1-15-76
1-16-76
1-17-76
1-16-76
1-19-76
1-20-76
1-21-76
1-22-76
1 -23-76
1-24-76
1-25-76
1-2 6-76
1-27-76
1-28-76
1-2 9-76
1-30-76
1-31-76
2- 1-76
2- 2-76
2- 3-76
2- 4-76
2- 5-76
2- 6-76
2- 7-76
2- 8-76
2 9-76
2-10-76
2-1 1- 76
2-12-76
2-13-76
2-14-76
0. 20 00
0.7000
0.5000
0.6000
0.9000
0.9000
0.7000
0.4000
0.7000
0.5000
0.6000
0.7000
0.6C00
S6. 67
93.00
87.5C
55.OC
90. 53
92.5C
90.67
96.OC
82.5C
94.44
88.00
90.OC
95. OC
7. 600
7. 500
7. 400
7. 5C0
7. 700
7. 400
7. 500
7. 400
7. 300
7. 200
7. 300
7. 3CO
7. 500
7. 700
7.600
7.500
7.700
8.000
7. 700
7. 700
7. 000
7.500
7.400
7.500
7.500
r.600
0.4000
0.2000
0.0
0.1000
0.1000
0.1000
0.3000
0.1000
0.2000
0.2000
0. 1000
0.2000
0.2000
0.2000
0.2000
93.33
98.00
99. 17
98.95
99.00
97. 50
98.67
98.00
95.00
98 .89
96.00
97.14
98.33
7. 6C0
7. 500
7.400
7.30C
7.800
7. 300
7.5C0
7.400
7.400
7.400
7. 300
7.50C
7.200
7.3C0
7.4C0
9. 200
8. 500
7. 800
8.500
8. 300
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 2 CF
PART 2 OF
04/06/77
DATE
OLD PR I EF
SET SOLIDS
IML/L)
10
P.C. REM.
SET SOLIDS
OLD P CLAR
11
OLD PRIM.
EFF. PH
(UNITS!
12
FILTEP fcFF
PH
(UNITS)
13
FINAL EFF
SET SOLIDS
(ML/LJ
14
PC OVERALL
SET SOLIDS
REMOVED
15
FINAL
EFFLUENT
PH (UNITS)
16
TRICK FILT
E t-F D.O.
( MG / L )
2-15-76
2-16-76
2-17-76
2-10-76
2-19-76
2-20-76
2-21-76
2-22-76
2-23-76
2-24-76
2-25-76
2-26-76
2-27-76
2-28-76
2-29-76
3- 1-76
3- 2-76
3- 3-76
3- 4-76
3- 5-76
3- 6-76
3- 7-76
3- 8-76
3- 9-76
3-10-76
3-11-76
3-12-76
3-13-76
3-14-76
3-15-76
3-16-76
3-17-76
3-18-76
3-19-76
3-20-76
3-21-76
3-22-76
3-23-76
3-24-76
3-25-76
3-26-76
3-27-76
3-28-76
3-29-76
3-30-76
0.7000
1.5C0
0.7000
0.5000
0.9000
0.7000
0.90C0
0.9000
0.7000
0.5000
0.7000
0.7000
0.5000
92.22
87.50
93.00
92.86
95. 26
94.17
87.14
91 .00
96.32
90.00
90.00
91.25
95.83
7. 200
7. 200
7. 500
7. 2 CO
7. 300
7. 400
7. 300
7. 500
7. 2CO
7. 400
8. 700
7. 600
7.400
7.400
7.500
7.500
7.400
7.600
7.500
7.600
7.500
7.300
7.500
7.400
7.600
8.300
7.700
7.600
0.2000
0 .0
0.2000
0.2000
0.2000
0.3000
0.5000
0.6000
0.5000
0.3000
0.5000
0.2000
0.2000
0.2000
0.3000
0.2000
97.78
98.00
97. 14
96.95
97.50
75.00
95.00
90.00
95.71
95.00
96.00
97. 14
96.25
98.33
7. 100
7. 300
7.400
7.20C
7. 500
7.300
7. 500
7.300
7. 100
7.400
7. 300
7.300
7.400
8. ICO
7. 500
7. 500
w :r: o j fv
-------
NEW HOLLANO, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 3 OF
PART 2 OF
9
6
04/06/77
DATE
OLD PR I EF
SEI SOLIDS
t ML/L I
10
P.C. REM.
SET SCLIDS
OLD P CLAR
11
OLD PRIM.
EFF. PH
(UNITS)
12
FILTER EFF
PH
(UNITS)
13
FINAL EFF
S EI SOL I OS
(ML/L »
14
PC OVERALL
SET SOLIOS
REMOVED
15
F INAL
EFFLUENT
PH (UNITSI
16
TRICK FI LT
EFF D.O.
(MG/L)
3-31-76
4- 1-76
4- 2-76
4- 3-76
4- 4-76
4 - 5 76
4 - 6 76
4- 7-76
4- 8-76
4- 9-76
4-10-76
4-11-76
4-12-76
4-13-76
4-14-76
4-15-76
4-16-76
4-17-76
4-18-76
4-19-76
4-20-76
4-21-76
4-22-76
4-23-76
4-24-76
4-25-76
4-26-76
4-27-76
4-20-76
4-29-76
4-30-76
5- 1-76
5- 2-76
5- 3-76
5- 4-76
5- 5-76
5- 6-76
5- 7-76
5- 8-76
5- 9-76
5-10-76
5-11-76
5-12-76
5-13-76
5-14-76
0.7000
0.2000
0.9000
0.7000
0.8000
1.000
0.6000
95.33
99 .00
7. 300
7.400
87.14
93.64
91.11
90.00
96.OC
7. 300
7. 500
7. 300
7. 200
7. 300
7. 200
7. 200
7. 500
7.500
7.500
7.400
7.600
7.700
7.200
7.500
7.400
7. 300
7.400
7.500
0.2000
0.2000
0.3000
0.2000
0.2000
0.3000
0.4000
0.3000
0.4000
0.1000
0.2000
0.2000
0.2000
0.2000
98.67
99.CO
97.00
97. 14
98.46
96.25
98. 10
98.93
97.50
98. 57
98.18
97.78
98.00
98.67
7.50C
7. 600
7.600
7. 300
7.6C0
7.4CC
7.2C0
7.2C0
7.500
7.200
7.20C
7. 300
7.300
7.200
7.200
7.400
7.200
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 4 OF 9
PART 2 OF 6
04/06/77
OATE
OLD PR I EF
SET SOLIDS
(ML/L)
10
P.C. REM.
SET SOLIDS
OLO P CLAP
11
OLD PRIM.
EPF. PH
(UNITS)
12
FILTER EFF
PH
(UNITSI
13
FINAL EFF
SET SOLIDS
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLF
PAGE 5 OF 9
PART 2 UP 6
04/06/77
9
10
11
12
13
14
15
OLO PRI EF
P.C. REM.
OLD PRIM.
FILTER EFF
FINAL EFF
PC OVERALL
FINAL
SET SOLIDS
SET SOL 10 S
EFF. PH
PH
SET SOLIDS
SET SOL IDS
EFFLUENT
DATE
(ML/L 1
OLD P CLAR
(UNITS)
(UMTS)
(ML/L)
REMOVED
PH (UN ITS)
6-29-76
_
_
7. 3CO
7.300
-
-
7.200
6-30-76
-
-
-
-
-
-
7- 1-76
-
-
7. 400
7.300
-
-
7.3C0
7- 2-76
-
-
-
-
-
-
~
7- 3-76
-
-
-
-
-
7- 4-76
-
-
-
-
-
-
7- 5-76
-
-
-
-
¦
-
7- 6-76
-
-
-
-
7- 7-76
-
-
-
-
-
-
7- 8-76
3. 500
50.00
6. 500
7.300
0.50C0
92.86
7.2CC
7- 9-76
3.0 00
70.OC
6. 600
6.900
0.5000
95.CO
7.0C0
7-10-76
-
-
-
-
-
-
~
7-11-76
-
-
-
-
-
-
7-12-76
1.500
87. 5C
6. 900
7.200
0. 5000
95.83
7. IOC
7-13-76
-
-
-
-
-
-
7-14-76
-
-
-
-
-
-
7-15-76
3.000
83. 32
6. 800
7.000
0.5000
97 .22
t. 9CC
7-16-76
1.500
85.OC
6. 700
7.400
0.3000
97.00
7 400
7-17-76
-
-
-
-
-
-
7-1B-76
-
-
-
-
-
7-19-76
-
-
-
-
-
-
~
7-20-76
-
-
-
-
-
-
7-21-76
1.500
75.00
6. 700
-
0.5000
91.67
7. ICO
7-22-76
1.200
86. 67
7. 000
7.600
0.3000
96.67
6.9CG
7-23-76
2.000
33. 33
6. 600
7.300
0.4000
86.67
7. ICO
7-24-76
-
-
-
-
-
-
7-25-76
-
-
-
-
-
¦
7-26-76
6.000
53.85
6. 600
7.500
0.2000
98 .46
7 . 2 C 0
7-27-76
0.5000
97.06
6. 500
7.300
0.2000
96.82
7.000
7-2 8-76
1.000
93.33
6. 700
6.800
0.4000
97.33
6. 800
7-29-76
1. 200
97. 6C
6. 400
6.900
0. 5000
99 .00
6. ecc
7-30-76
0.6000
94.OC
6. 600
6.700
0.5000
95.00
6.8C0
7-31-76
-
-
-
-
-
-
~
8- 1-76
-
-
-
-
-
-
8- 2-76
1.000
87.50
6. 900
-
0.4000
95.00
6.900
8- 3-76
0.4000
94.67
7. 000
7.400
0.1000
98.67
7. ICC
8- 4-76
1.000
90.00
7. 300
7.400
0.3000
97.00
7.000
8- 5-76
1.000
90.OC
7. 000
-
0.3000
97 .00
6. 800
8- 6-76
0.8000
90.CO
7. 300
7. 100
0.2000
97.50
7.000
8- 7-76
-
-
-
-
-
-
8- 8-76
-
-
-
~
-
-
8- 9-76
0.7000
88.33
7. 100
6.800
0.2000
96.67
7. 000
B-LO-76
1.500
81.25
7. 300
7. 100
0.0 T
-
7.200
8-11-76
1.600
80.OC
6. 900
7.000
0.2000
97.50
7. 000
8-12-76
1. 100
89.OC
6. 400
7.000
0.4000
96.CO
6. 7C0
16
TRICK FlLT
EFF 0.0.
(MG/L)
3.COO
1. 800
2.500
2. 800
3.600
2. 300
5. '.00
3.200
2. 700
3.400
2.200
3. 800
4. 900
2.900
5.00 0
'..2 00
2.200
2. 500
2. 100
3. 500
I
I
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT PAGE 6 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 2 OF 6
DATA TABLE
04/06/77
9
1C
11 .
12
13
14
15
16
OLD PRI EF
P.O. REM.
OLD PRIM.
FILTER EFF
FINAL EFF
PC OVERALL
F INAL
TRICK 1
SET SOLIDS
SET SOLIDS
EFF. PH
PH
SET SOLIDS
SET SOLIDS
EFFLUENT
EFF D
DATE
(HL/L )
OLD P CLAR
(UMIS)
(UNITS!
(ML/L)
REMOVED
PH (UNITS)
< MG /
8-13-76
1.50C
75.00
6. 400
7. 100
0.4000
93.33
fc. 800
2.200
8-14-76
-
-
-
-
-
-
-
-
8-15-76
-
-
-
-
-
-
-
-
8-16-76
-
-
-
-
-
-
-
8-17-76
1 .400
89.23
6. 200
7. 100
0.4000
96.92
6. eco
4. 3 00
8-18-76
-
-
-
-
-
-
-
-
8-19-76
0.5000
95. 83
5. 900
6.900
0.1000
99. 1 7
6. 7C0
4.2 00
8-20-76
1.500
89.29
6. 700
7. 100
0.1000
99. 29
6. 900
2.600
8-21-76
-
-
-
-
-
-
-
-
8-22-76
-
-
-
-
-
-
-
-
8-23-76
0.5000
92. 8fc
6. 900
7.000
0.10C0
98.57
fc. 800
2.600
8-24-76
-
-
-
-
-
-
-
-
8-25-76
1.800
80.OC
6. 9C0
7.400
0.2000
97.76
7. 200
2.000
8-26-76
1.000
87. 5C
6. 700
7.300
0.20C0
97.50
6.6CC
4. 000
8-27-76
0.4000
-
6. 800
7. 800
0.1000
-
7. 100
1.600
8-28-76
-
-
-
-
-
-
-
-
8-29-76
-
-
-
-
-
-
-
-
8-30-76
1.300
87.00
6. 600
7.600
0.0 T
-
6. 800
4. 500
8-31-76
0 .8000
91.11
6. 700
7.300
0.2000
97. 78
6.900
4.COO
9- 1-76
0.7000
94.17
6. 200
7.500
0.2000
98.33
fc. 900
4.900
9- 2-76
0.8000
86.67
6. 800
7. 200
0.2000
96.67
6.900
3.600
9- 3-76
1.800
82.86
6. 700
7.300
0.2000
98. 10
7.000
4. 500
9- 4-76
-
-
-
-
-
-
-
-
9- 5-76
-
-
-
-
-
-
-
-
9- 6-76
-
-
-
-
-
-
-
-
9- 7-76
1.200
86.6 1
6. 700
T. 300
0.2000
97 .78
fc. 8C0
5. 000
9- 8-76
1.000
86.67
6. 900
7. 200
0.2000
97.33
6.900
4.900
9- 9-76
1.200
85.OC
6. eco
7.200
0.3000
96.25
6. 7CC
3. 900
9-10-76
0.7000
91.76
6. 700
7.400
0.2000
97.65
7.000
3. 700
9-11-76
-
-
-
-
-
-
-
-
9-12-76
-
-
-
-
-
-
-
-
9-13-76
1.000
89.47
7. 100
7.400
0.2000
97 .69
7.0C0
3. ] 00
9-14-76
1.000
86.67
7. 100
7.200
0.1000
98 .67
7.000
4.200
9-15-76
0.9000
88.75
7. 000
7.300
0.2000
97.50
7.00C
3. 600
9-16-76
-
-
-
-
-
-
-
-
9-17-76
0.5COO
93.75
7. 000
7.500
0.0 T
-
7. OCO
3.200
9-18-76
-
-
-
-
-
-
-
-
9-19-76
-
-
-
-
-
-
-
-
9-20-76
-
-
-
-
-
-
-
-
9-21-76
-
-
-
-
-
-
-
-
9-22-76
-
-
-
-
-
-
-
-
9-23-76
-
-
-
-
-
-
-
-
9-24-76
-
-
-
-
-
-
-
-
9-25-76
-
-
-
-
-
-
-
-
9-26-76
-
-
-
-
-
-
-
-
r<>> > i
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 7 OF 9
PART 2 OF 6
04/06/77
OATE
OLO PR 1 EF
SET SOLIDS
< ML/L I
10
P.C. REM.
SET SOLIDS
OLO P CLAR
11
OLO PRIM.
EFF. PH
(UNITS)
12
FILTER EFF
PH
CUMTS)
13
FINAL EFF
SET SOLIDS
(ML/L)
1".
PC OVERALL
SET SOLIDS
REMOVED
15
FINAL
EFFLUENT
PH (UNITS)
16
TRICK F 1 LT
EFF D.O.
( MG / L I
9-27-76
9-28-76
9-29-76
9-30-76
10- 1-76
10- 2-76
10- 3-76
10- 4-76
10- 5-76
10- 6-76
10- 7-76
10- 8-76
10- 9-76
10-10-76
10-11-76
10-12-76
10-13-76
10-1 A-76
10-15-76
10-16-76
10-17-76
10-18-76
10-19-76
10-20-76
10-21-76
10-22-76
10-23-76
10-24-76
10-25-76
10-2C-76
10-2 7-76
10-28-76
10-29-76
10-30-76
10-31-76
- l-7b
- 2-76
- 3-76
- 4-76
- 5-76
- 676
- 7-76
- 8-76
- 9-76
-10-76
0.9000
0.5000
1. 2C0
0.7000
1 .400
1.UC0
1.200
0.bOOO
0.4000
1.500
0.7000
0.6000
95. 5C
93.75
88.00
88.33
86.00
90.00
87.37
92.00
96. 3fc
86.36
92.22
S5.36
6. 800
7. ICO
7. 300
7. 3 00
7. 100
7. 300
7. 500
7. 700
7. 100
7. 100
7. 500
7. 500
7. 700
7.700
7.500
7. 800
7.600
2000
1000
10C0
7.300
7.700
7.500
7.800
8.000
7.800
7.600
7. 700
7. 700
7. 600
7. 900
7. 700
0.0
2000
2000
2000
1000
2000
0 .1000
0.0
0. 1000
0.10C0
0.1000
0.4000
0.0
0.0
0.0
o.iooo
0.1000
0.1000
0 .0
0.1000
0.1000
0.1000
0. 1000
97.89
99.38
99. 33
98.00
98.82
98. 18
99 . 17
97.65
98.89
98.82
99.33
99.00
98.00
99.00
99.00
98.95
99.09
99 .09
98.89
99.23
7.200
7.20C
7. ICO
7.300
7.200
3. 5CC
4. ICO
3. 6C0
4. ICO
7. 400
7.200
7. 50C
7.400
7.5C0
7. 50C
7. 300
7.400
7.300
7. 200
7.40C
7.400
5.100
5. 200
5.000
3. 500
4. 000
4.300
3.GOO
3. 5 00
3.400
6.400
6.6 00
6. 500
6. 300
4. 500
5.700
5.<»00
4.COO
3.500
4. 4 00
4.400
4.000
3.800
3, 000
4.200
5. 800
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 8 CIF 9
PART 2 OF 6
04/06/77
DATE
OLD PRI EF
SET SOLIDS
(ML/L)
10
P.O. REM.
SET SOLIDS
OLD P CLAR
11
OLD PRIM.
EFF. PH
(UNITS)
12
FILTER EFF
PH
(UNITS)
13
FINAL EFF
SET SOLIOS
(ML/L)
14
PC OVERALL
SET SOLIDS
REMOVED
15
FINAL
EFFLUENT
Ph (UNITSI
lb
TRICK FILT
EFF D.O.
(MG/LI
11-11-76
11-12-76
11-13-76
11-14-76
11-15-76
11-16-76
11-17-76
11-18-76
11-19-76
11-20-76
11-21-76
11-22-76
11-23-7b
11-2 4-76
11-25-76
11-26-76
11-27-76
11-28-76
11-29-76
11-30-76
12- 1-76
12- 2-76
12- 3-76
12- 4-76
12- 5-76
12- 6-76
12- 7-76
12- 8-76
12- 9-76
12-10-76
12-11-76
12-12-76
12-13-76
12-14-76
12-15-76
12-16-76
12-17-76
12-18-76
12-19-76
] 2 -20- 76
12-2 1-76
12-22-76
12-23-76
12-24-76
12-25-76
0.9000
0.5000
0.6000
1. 100
0.5COO
2 .000
1 .000
0.7000
0.5000
0. 1000
0.7000
0.9000
1.000
93. oe
96. 1 5
96.25
90.OC
96. 15
61.82
94.44
91.25
96.43
59.33
52.22
68.75
88.24
7. 600
7.400
7. 500
7. 400
7. 400
7. 400
7. 5 00
7. 600
7. 300
7. 500
7. 4CO
7. 400
7. 300
7.600
7.900
7.600
7.700
7.800
71 900
7.800
7.500
7. 500
7.600
7.500
0.0
0. 1000
0.1000
0.3000
0.0
0. 1000
O.C
0. 1000
0.2000
0.0
99.23
99.36
97.27
99.29
98.89
97.50
7.4CC
7.2C0
7.30C
7.4CC
7.300
6. ICO
7.100
6.600
7. 500
7. 3C0
7.300
7. 100
7. 30C
4. 100
4.200
4. 400
3. 800
3. 500
-------
NEW HCLLAND, PA WASTEWATER TREATMENT PLANT PAGE 9 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 2 OF 6
OAT A TABLE
04/06/77
DATE
OLD PRI EF
SET SOLIDS
(ML/L )
1C
P .C . REM.
SET SOLIDS
OLD P CLAR
11
OLD PRIM.
EPF. PH
(UNITS)
12
FILTER EFF
PH
-------
NEW HGLLAND, PA WASTEWATER TREATMENT PLANT PAGE 1 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PAHT 3 OF 6
DATA TABLE
04/06/77
OATE
17
FINAL EFF
0.0 .
(MG/LI
16
FINAL EFF
BOOl5 DAY)
(MG/L)
19
PERCENT
OVERAL BOD
REMUVED
20
FINAL EFF
SUS SOLIDS
(MG/L I
21
PERCENT
OVERALL SS
REMOV ED
22
CHLOR1NE
USED
PUUNDS/DAY
23
CHLORINE
RESIDUAL
(MG/LI
24
DIGESTER
SUPT PH
(UNITSI
1- 1
1- 2
1-
1-
1-
1-
1-
1-
1-
1-10
1-11
1-12
1-13
1-14
1-15
1-16
1-17
1-18
1-19
1-20
1-21
1-22
1-23
1-24
1-25
1-26
1-27
1-28
1-29
1-30
1-31
2- 1
2-
2-
2-
2-
2-
2-
2-
2-
2
2
3-
4
5
6
7
8
9
-10
2-11
2-12
2-13
2-14
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
-76
9.000
9. 100
15.OC
34. OC
87. C7
84.40
11.50
28 .00
42 .00
85.86
82.35
9.300
9.200
65.00
29.OC
74. 81
25 .00
23 .CO
88.32
43.OC
62. 16
30.00
40 .00
40.00
35.00
35 .00
40 .00
30 .00
30 .00
30 .00
30.00
30 .00
35.00
30.00.
35.00
35.00
35.00
35.00
35.00
30.00
35.00
35.00
40.00
35.00
35.00
30 .00
30.00
35.00
35 .00
35.00
35.00
35.00
30.00
30.CO
50.00
50.00
60 .00
60.00
60 .00
30.00
1. CCC
0.8000
0.6000
5C00
8CC0
6000
0.2000
0.4CO0
0.3000
C. 2000
0.6000
0.5000
C.4000
0.5CC0
0.4000
0.5000
C.5CC0
0.60CC
0.5000
C.40C0
5000
6C00
40C0
7000
40CO
3C00
1C00
5CCC
4000
3000
5. 900
6. 300
6. 300
6. 300
6. ICO
6. 100
6. 100
6. 100
6. 100
5.600
'< i > I
-------
NEW HOLLAND. PA WASTEWATER. TREA1MENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 2 OF
PART 3 Of
9
6
04/06/77
DATE
17
FINAL EFF
0.0.
(MG/LI
ie
FINAL EFF
000(5 OA YI
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PACE 3 OF 9
PART 3 OF 6
04/06/77
DATE
17
FINAL EFF
0 .0 .
(MG/L t
ie
FINAL EFF
BOQ(5 DAY I
(MG/L)
19
PERCENT
OVERAL BOO
REMOVED
20
FINAL EFF
SUS SOLIDS
(MG/L)
21
PERCENT
OVERALL SS
REMOVED
22
chlorine
US EO
POUNDS/DAY
23
CHLOP!NE
RESIDUAL
(MG/LI
24
DIGESTER
S UP T PH
(UNI TS»
3-31-76
4- 1-76
4- 2-76
4- 3-76
4- 4-76
4- 5-76
4- 6-76
4- 7-76
4- 0-76
9-76
4-10-76
4-1 1-76
4-12-76
4-13-76
4-14-76
4-15-76
4-16-76
4-17-76
4-16-76
4-19-76
4-20-76
4-21-76
4-22-76
4-23-76
4-24-76
4-25-76
4-26-76
4-27-76
4-28-76
4-29-76
4-30-76
5- 1-76
5- 2-76
5- 3-76
5- 4-76
5- 5-76
5- 6-76
5- 7-76
5- 0-76
5- 9-76
5-10-76
5-11-76
5-12-76
5-13-76
5-14-76
35.OC
02.23
45.OC
40.OC
28.OC
22.00
36 .00
81.78
79. 31
82. 39
78.22
04.35
33.00
28.00
36.00
31.00
8.000
37.00
83.82
84.27
78.57
85.17
80.32
28.00
82 .39
tO .00
60 .00
60.00
30 .00
40.00
50 .00
50.00
50.00
40.00
30.00
40.00
40 .00
40.00
40.00
40 .00
30.00
30.00
40.00
40 .00
40.00
40.00
40.00
30.00
30 .00
40.00
40.00
40.00
40.00
40.00
30.00
30.00
30.00
30.00
30.00
30 .00
30 .00
30.00
30.00
30 .00
30.00
30.00
0.5000
C 4000
0. 5000
C.3000
0.6000
C.7000
0.6000
0.5000
0.50CO
0.4000
0.50C0
0.2000
0.3000
C.4C00
0.50CC
0.3000
0.5000
0.6000
0.3C00
0.5000
0.2000
0.5000
0.4C00
0.4000
0. 5CG0
0.300C
0.5000
0.4000
0.3000
C.4CC0
0.50C0
0.5000
5. 400
-------
NEIrf HGLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGL- « OF 9
PART 3 OF 6
04/06/77
DAT E
17
FINAL EPF
O .0 .
(MG/L)
1 e
FINAL EFF
600(5 DAY)
MG/L)
19
PERCENT
OVEPAL 000
RE MOVE 0
20
FINAL EFF
SUS S OLIOS
ICG/L)
21
PERCENT
OVERALL SS
REMOVED
22
CHLORINE
USED
POUNDS/DAY
23
CHLORINE
RESIDUAL
(MG/LI
2*
DIGESTER
SUPT PH
( UNI TSI
5-15-76
5-16-76
5-17-76
5-18-76
5-19-76
5-20-76
5-21-76
5-22-76
5-23-76
5-24-76
5-25-76
5-26-76
5-27-76
5-28-76
5-29-76
5-30-76
5-31-76
6- 1-76
6- 2-76
6- 3-76
6- 4-76
6- 5-76
6- 6-76
6- 7-76
6- 6-76
6- 9-76
6-10-76
6-11-76
6-12-7b
6-13-76
6-14-76
6-15-76
6-16-76
6-17-76
6-18-76
6-19-76
6-20-76
6-21-76
0-22-76
6-23-76
6-24-76
6-25-76
6-26-76
6-27-76
6-28-76
27.OC
39.OC
34.00
44.CO
13.00
11.00
94.32
3 1.00
73.47
eo. 57
29.00
47.00
69. 23
9 7. 34
56.00
39.00
24.00
90. 91
85.55
71.64
8 1 .20
7 6.76
79 .26
85.96
30 .00
30.00
30 .00
30.00
30 .00
30 .00
30.00
30.00
30.00
30.00
30.00
30 .00
30 .00
30.00
30.00
30.00
30.00
30.00
30 .00
30.00
30.00
30 .00
30.00
30.00
30.00
30.00
30.00
30.00
30.CO
30.00
30.00
30 .00
30.'OO
30.00
30 .00
30.00
30.00
30.00
30 .00
30.00
30.00
30.00
30.00
30.00
0.6000
0.40CC
0.5C00
0.3000
0.4000
0.5000
0.400C
0.3000
0.4000
0.3CCC
0.40CO
0.4000
C.5C00
C.5CG0
0.3000
0.4CC0
C.60CO
0.40C0
5000
4000
5000
3000
4CCC
0.40C0
C.40C0
0.5000
0.3CC0
0.4CC0
0.7000
5.400
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 5 OF 9
PART 3 OF 6
0't/06/7 7
OATE
17
FINAL eff
D.O.
(MG/LI
18
FINAL EFF
BOD< 5 DAY)
(MG/LI
19
PERCENT
OVERAL BOD
REMOVED
20
FINAL EFF
SUS SOLIDS
(MG/L)
21
PERCENT
OVERALL SS
REMOV ED
22
CHLORINE
USED
POUNDS/DAY
23
CHLORINE
RESIDUAL
(MG/L)
24
DIGESTER
Sl'PT PH
(UNITS)
6-29-76
-
-
-
-
-
30 .00
0.5000
-
6-30-76
-
31.00
86.04
34.00
81.62
30.00
C.40CC
-
7- 1-76
-
-
-
-
-
30.CO
0.40C0
-
7- 2-76
-
-
-
-
-
30.00
-
-
7- 3-76
-
-
-
-
-
30.00
-
-
7- A-76
-
-
-
-
-
30.00
-
-
7- 5-76
-
-
-
-
-
30.00
0.4000
-
7- 6-76
-
-
-
-
30.00
0.5000
-
7- 7-76
-
-
-
-
-
30.00
0.4000
-
7- 6-76
-
-
-
31 .00
82.58
40.00
C.6CC0
-
7- 9-76
5.100
37. OC
82.55
-
-
40.00
0.40C0
-
7-10-76
-
-
-
-
-
-
-
-
7-11-76
-
-
-
-
-
-
-
-
7-12-76
-
-
-
30.00
80 .26
40.00
0.4CCO
-
7-13-76
-
-
-
-
-
40.00
0.3000
-
7-14-76
-
-
-
-
-
40.00
0.50C0
-
7-15-76
6 .500
-
-
-
-
6C .CO
0.6CC0
-
7-16-76
5.200
47.OC
-
-
-
40.00
0.4000
-
7-17-76
-
-
-
-
-
-
-
-
7-18-76
-
-
-
-
-
-
-
-
7-19-76
-
-
-
-
-
40.00
G.6CC0
-
7-20-76
-
-
-
-
-
40.00
0.600C
-
7-21-76
4.500
-
-
-
-
40.00
0.8CC0
-
7-22-76
5.200
-
-
-
-
35.00
G.6C00
-
7-23-76
5.800
33.OC
93.28
-
-
-
-
-
7-24-76
-
-
-
-
-
-
-
-
7-25-76
-
-
-
-
-
-
-
-
7-26-76
6 .000
-
-
-
-
35.00
0.3CCC
-
7-27-76
3 .900
-
-
-
-
80.00
1.000
G
-
7-20-76
4.500
-
-
102.0
-2.000
60.00
l.COC
G
-
7-29-76
4.600
-
-
97.00
88 .67
60.00
l.OCC
G
-
7-30-76
7.100
50.OC
71.91
-
-
60.00
1.000
G
-
7-31-76
-
-
-
-
-
-
-
-
8- 1-76
-
-
-
-
-
-
-
-
8- 2-76
6 .000
-
-
7.000
98 .26
50.00
l.OGO
G
-
8- 3-76
4.900
-
-
7.000
93.00
50.00
0.6000
-
8- 4-76
6.100
-
-
- ¦
-
50.00
0.40C0
-
0- 5-76
7 .900
-
-
-
-
50.00
l.CCO
G
-
8- 6-76
7.800
64.00
57.33
-
-
50.00
1.000
G
-
8- 7-76
-
-
-
-
-
-
-
-
8- 8-76
-
-
-
-
-
-
-
-
8- 9-76
5.200
-
-
7.000
9 2.71
50.00
l.OCC
G
~
8-10-76
5.400
-
-
5.000
95.15
50.00
C.10C0
6 . 600
8-11-76
5.000
-
-
14.00
86.67
60 .CO
1.000
G
-
8-12-76
5 .700
-
-
15.00
89.51
60.CO
l.OCC
G
-
-------
NEV« HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 6 OF 9
PART 3 OF 6
04/06/77
DAT E
17
FINAL EFF
0.0 .
IMG/L)
1 6
FINAL EFF
000( 5 DAY I
(MG/H
19
PERCENT
OVERAL BOO
REMOVED
20
FINAL E»;F
SUS SOLIDS
(fG/L)
21
PERCENT
OVERALL SS
REMOVED
22
CHLOR INE
usto
POUNDS/DAY
23
CHLORINE
RESIDUAL
(MG/LI
24
DIGESTER
SUPT PH
(UNITS1
8-13-76
4,600
25.00
84.28
25.00
71.59
40.00
o
o
-
8-14-76
-
-
-
-
-
-
-
-
8-15-76
-
-
-
-
-
-
,
-
8-16-76
-
-
-
-
-
-
-
-
8-17-76
5.400
-
-
15.00
-
50.00
1.000
G
-
8-18-76
-
-
-
-
-
-
-
-
8-19-76
6 .400
-
-
1.000
99.46
40.00
1.000
G
-
6-20-76
5 .500
28.00
69. S6
17 .00
90.86
40.00
1.000
G
-
8-21-76
-
-
-
-
-
-
-
-
8-22-76
-
-
-
-
-
-
-
-
8-23-76
5.500
-
-
22.00
9 2. 14
30.00
0.3000
-
8-2'i-76
-
-
-
-
-
40.00
-
-
8-25-76
5.500
-
-
19.00
84.43
45.00
0.7COO
-
8-26-76
5.400
-
-
16.00
90.12
45.00
1.000
G
-
8-27-76
5.100
18.OC
80.22
-
-
45.00
1.0C0
G
-
8-26-76
-
-
-
-
-
45.00
-
-
8-29-76
-
-
-
-
-
45.00
-
-
8-30-76
7.400
-
-
11.00
91.13
45.00
1.000
G
-
8-31-76
6 .400
-
-
13.00
93.66
45.00
1.000
G
-
9- 1-76
5.600
-
-
3.000
98.35
45.00
l.COO
G
-
9- 2-76
5.500
-
-
13.00
90.71
45.00
1.000
G
-
9- 3-76
6 .200
-
-
15.00
94.93
45.00
l.COO
G
-
9- 4-76
-
-
-
-
-
-
-
-
9- 5-76
-
-
-
-
-
-
-
-
9- 6-76
-
-
-
-
-
-
-
-
9- 7-76
6 .000
-
-
13.00
92.22
45.00
l.COO
G
-
S- 8-76
6.300
-
-
5.000
96.21
40.00
1.000
G
-
9- 9-76
5.600
-
-
11.00
89.22
40.00
l.CCO
G
-
9-10-76
5 .400
12.00
92. 55
11.00
93.89
40.00
0.6000
-
9-11-76
-
-
-
-
-
-
-
-
9-12-76
-
-
-
-
-
40.00
-
-
9-13-76
5.600
-
-
11.00
89.22
40.00
0.9000
-
9-14-76
6.400
-
-
6.000
94.34
40.00
l.CCO
G
-
9-15-76
5.800
-
-
5.000
97.19
40.00
1.000
G
-
9-16-76
-
-
-
-
-
40.00
-
-
9-17-76
4.600
36.00
87. 14
12.00
92.59
4C .00
l.CCO
-
9-18-76
-
-
-
-
-
40.00
-
-
9-19-76
-
-
-
-
-
-
-
-
9-20-76
-
-
-
-
-
-
-
-
9-21-76
-
-
-
-
-
40.00
-
-
9-22-76
-
-
-
-
-
40.00
-
7. 000
9-23-76
-
-
-
-
-
40.00
-
6. 900
9-24-76
-
52.OC
64. 34
-
-
40 .00
-
-
9-25-76
-
-
-
-
-
40.00
-
-
9-26-76
-
-
-
-
-
40.00
-
-
-------
MEW HOLLANDf pa WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DAT A T ABLE
PAGE 7 Or- 9
PART 3 OF 6
04/06/77
17
ie
19
20
21
22
23
2 4
FINAL EFF
FINAL EFF
PERCENT
FINAL EFF
PERCENT
CIILOR INE
CHLORINE
DIGES
D.O.
BOO(5 DAY)
OVERAL BOD
SUS SOLIDS
OVERALL SS
USED
RESIDUAL
SUPT
DATE
(MG/L »
(MG/L)
REMOVED
(MG/L)
REMOVED
POUNDS/DAY
(MG/L)
( UN
9-27-76
6 .200
_
14.00
_
40.00
l.CCO
G
6. <500
9-28-76
6.600
-
-
14.00
-
40.00
1.000
G
7. 000
9-29-76
5.200
-
-
17.00
-
40.00
1 .000
G
6. 800
9-30-76
-
-
-
-
-
40.00
-
-
10- 1-76
5 .800
26. OC
-
19.00
-
40.00
0.9000
6. 800
10- 2-76
-
-
-
-
-
-
-
-
10- 3-76
-
-
-
-
-
-
-
-
10- 4-76
5.200
-
-
16.00
94. 54
40.00
1.000
G
7.200
10- 5-76
5.700
-
-
15.00
9 1.94
40.00
l.OCC
G
7.200
10- 6-76
5.900
-
-
13.00
94.20
40.00
C. 7000
6. 900
10- 7-76
5 .900
-
*
u.oo
95.18
40.00
1.000
G
6. 800
10- 8-76
6. 200
28.00
86. 60
12.00
95.4?
40.00
0.5000
6. 800
10- 9-76
-
-
-
-
-
-
-
-
10-10-76
-
-
-
-
-
35.00
-
-
10-11-76
-
-
-
20.00
92.37
35.00
0.60C0
-
10-12-76
-
-
-
10.00
96. 40
35.00
0.8000
-
10-13-76
-
-
-
9.000
95.36
40 .00
1.000
G
6. 700
10-14-76
-
-
-
10.00
96.35
4C.00
1.000
G
-
10-15-76
-
53.00
-
-
-
40 .00
I. 000
G
-
10-16-76
-
-
-
-
-
40.00
-
-
10-17-76
-
-
-
-
-
40.00
-
-
10-18-76
7.400
-
-
9,000
96.37
40.00
1.000
G
-
10-19-76
-
-
-
-
-
40 .00
-
-
10-20-76
6.900
-
-
26.00
92.61
4 0.00
C.9000
-
10-21-76
6.200
-
-
10.00
94.74
40.00
1. 000
G
-
10-22-76
6.500
30.00
92. 13
13.00
94.49
40.00
C.8CC0
soo
10-23-76
-
-
-
-
-
-
-
-
10-24-76
-
-
-
-
-
40.00
-
-
10-25-76
-
-
-
-
-
40 .00
-
7.000
10-2 6-76
6 .200
-
-
13.00
94.96
40.00
0.6000
6. 900
10-2 7-76
4 .400
-
-
20.00
94.74
40.00
0.0
6. 900
10-28-76
6.3 00
-
-
24.00
89 .47
60.CO
0.20C0
6.900
10-29-76
5 .700
54.OC
84 87
16.00
94.24
70.00
1.000
G
6.900
10-30-76
-
-
-
-
-
40 .00
-
-
10-31-76
-
-
-
-
-
4C .00
-
-
11- 1-76
6 .800
-
-
9. 000
97.08
40.00
0. 70C0
-
11- 2-76
-
-
-
-
-
40.CC
-
-
11- 3-76
-
-
-
-
-
40 .00
-
-
11 - 4-76
-
-
-
-
-
40 .00
-
-
11- 5-76
4.300
39.OC
92. 14
36.00
93.05
40.00
0.50C0
6.800
11- 6-76
-
-
-
-
-
40 .00
-
-
11- 7-76
-
-
-
-
-
40 .00
-
-
11- 0-76
7 .000
-
-
14.00
96.00
40.00
0.30CC
6. 800
11- 9-76
6 .600
-
-
14.00
93.20
40.00
0.8CC0
6 . 800
11-10-76
-
-
-
17.00
92.34
40.00
0.7CC0
-
-------
NEW HOLLAND. PA WAS 1fcW AT ER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 8 OF 9
PART 3 OF 6
04/06/77
OATE
17
FINAL EFF
D .0 .
(MG/L)
18
FINAL EFF
BOD{5 DAY)
(MG/L1
19
PERCENT
OVERAL BOD
REMOVED
20
F I NAL EFF
SUS SOLIDS
(MG/L)
21
PERCEN1
OVERALL SS
REMOVED
22
CHLORINE
USED
POUNDS/DAY
23
CHLOR INE
RESIDUAL
(MG/LI
24
OIGESTER
SUP1 PH
(UNITSI
ll-l 1-76
11-12-76
11-13-76
11-14-76
11-15-76
11-16-76
I 1-17-76
11-18-76
11-19-76
11-20-76
11-21-76
11-22-76
11-23-76
11-24-76
11-25-76
11-26-76
11-27-76
11-20-76
11-29-76
11-30-76
12- 1-76
12- 2-76
12- 3-76
12- 4-76
12- 5-76
12- 6-76
12- 7-76
12- 8-76
12- 9-76
12-10-76
12-11-7&
12-12-76
12-13-76
12-14-76
12-15-76
12-16-76
12-17-76
12-16-76
12-19-76
12-20-76
12-21-76
12-22-76
12-23-76
12-24-76
12-25-76
7.500
8 .000
7.500
43.00
6 .000
6 .800
6 .300
7.600
6.700
66.00
84. 58
20.00
23.00
28.00
27.00
48.00
44 .00
33 .00
32 .00
28.00
94.44
93. 78
92.51
94.05
9 1.58
89.63
40.00
40.00
40 .00
40.00
40 .00
40.00
40.00
40.00
40.00
40 .00
40.00
40 .00
40.00
40 .00
40 .00
40 .00
40 .00
40.00
40.00
40.00
40.00
40.00
40 .00
40.00
40.00
40.00
40 .00
40.00
40.00
40 .00
50.00
50.00
50.00
50 .00
50.00
50.00
40.00
60.00
60.00
60 .00
60 .00
60.00
60.00
0.4000
l.COO G
0.9CCC
0.8000
0.8000
0.8000
0.5C00
0.5CC0
C.40CO
0.5000
0.4000
0.7000
1.000
l.OCO
l.OCO
G
G
G
-------
NEW HOLLAND, PA WASTEWATER TP E ATM ENT PLANT PA^E 9 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 3 OF 6
DATA TABLE
04/06/77
DAT E
17
FINAL EFF
0.0 .
IMG/L)
18
FINAL EFF
BOO(5 DAY I
(HG/L I
19
PERCENT
OVERAL BOD
REMOVED
20
FINAL EFF
SUS SOLIDS
(WG/L)
21
PERCENT
OVERALL SS
P.EMUV ED
22
CHLORINE
USED
POUNDS/DAY
23
CHLORINE
RESIDUAL
(MG/L1
24
DIGESTER
SuPT PH
(unirst
12-26-76
12-27-76
12-28-76
12-29-76
12-30-76
12-31-76
6 .SCO
7.200
6.200
7. 100
47. OC
92. 41
30.00
33 .00
35.00
24.00
90 .74
82.26
85.77
88.89
60.00
60.00
60.00
60.00
1. CCO
1.000
l.CCO
l.OOC
6.4 00
6.400
6.400
MlNIMUM
MAXIMUM
AV ERAGE
STD.DEV.
VLD.PTS.
3.900
U. 50
6 .233
1 .310
79
11.00
66. 00
37.63
14. 77
4C
57.33
97.34
03. 78
8. 155
33
1.000
102.0
23.31
16.59
93
-2.000
99.46
88 . 59
12.08
79
30.00
100.0
41.28
11.75
320
0.0
1.000
0.5881
0.2658
218
5.400
7. 200
6. 551
0.4753
37
NOTE - ( I SEE FOOTNOTE TABLE.
* SEE COMMENT TABLE.
T.G.L. OR Q = TRACE. GREATER
THAN. LESS THAN, OR QUESTIONABLE OATA.
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PL ANT
OPERATING REPORT 01/01/76 - 12/31/76
DAT A T A0LE
PAGE 1 GF 9
PART A OP 6
04/06/77
DATE
25
DIG SUPT
SET SOLIDS
(ML/L )
26
FECAL
COL I FORM
(ORG. /100I
27
SLUDGE
HAliLED
< GAL.»
20
P.C. TOTAL
SOL. SLDGE
HAULEO
29
PERCENT
VOLAT I L E
SOL I OS
30
Phi OF
SLUDGE
HAUL ED
31
DET. TIMt
NEW PRIM.
CLAR (HRSI
32
DET. TIME
OLD PRIM.
CLAR (HRSI
i- 1-76
1- 2-76
1- 3-76
I- 4-76
1- 5-76
1- 6-76
1- 7-76
1- B76
1- 9-76
1-10-76
1-1 1-76
1-12-76
1-13-76
1-14-76
1-15-76
1-16-76
1-17-76
1-18-76
1-19-76
1-20-76
1-21-76
1-22-76
1-2 3-76
1-24-76
1-25-76
1-26-76
1-27-76
1-28-76
1-29-76
1-30-76
1-31-76
2- 1-76
2- 2-76
2- 3-76
2- 4-76
2- 5-76
2- 6-76
2- 7-76
2- 8-76
2- 9-76
2-10-76
2-11-76
2-12-76
2-13-76
2-14-76
6.000
2.000
2.000
2.000
5 .000
10.00
7.000
7.000
3.000
6800.
3.00 0 L 6000.
5100.
2400. G
10.00 8500.
4.800
5.600
5.600
75.00
75.00
75.00
C.O
30. OC
C.O
2. 799
2.758
2.643
3.339
2. 758
2.719
2.883
2.680
2. 840
3.806
3.398
2.643
2.321
2. 799
2. 799
2.680
3.524
3.398
46.00
1.113
1. 106
2. 840
2. 643
. 799
.339
.339
.928
.762
3.06 9
3. 398
2. 799
5. 767
3.339
3.398
3.524
3. 172
5. 143
3. 120
4. 879
5. 767
3. 8C6
3.660
3. 96 5
3. 731
3 660
5.43 7
3.676
3.62 3
472
3Rb
623
571
700
521
731
5.000
4 4 6't
3.4 72
3.049
3.676
3. 676
3.521
4.630
4.464
1 .462
1.453
3. ?31
3.4 72
3.676
4.38b
4.386
3. 046
2.315
4. 032
4.4 64
3. 676
7.5 76
4.3 86
4.464
4.630
4.167
6. 757
4.098
410
576
000
60U
200
902
GOB
7. 143
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 2 OF 9
PART 4 CIF 6
04/06/77
DATE
25
D IG SUPT
SET SOLIDS
(ML/L )
26
FECAL
COL I FOR M
(ORG. /100I
27
SLUDGE
HAULEO
(GAL.)
28
P.C. TOTAL
SOL. SLOGE
HAULEO
29
PERCENT
VOLATILE
SOL IDS
30
PH OF
SLUDGE
HAULED
31
OET. TIME
NEW PRIM.
CLAR (HRS)
32
DET. I I ME
OLD PRIM.
CLAP (HRSl
2-15-76
2-16-76
2-17-76
2-18-76
2-19-76
2-20-76
2-21-76
2-22-76
2-23-76
2-24-76
2-25-76
2-26-76
2-27-76
2-20-76
2-29-76
3- 1-76
3- 2-76
3- 3-76
3- 4-76
3- 5-76
3- 6-76
3- 7-76
3- 8-76
3- 9-76
3-10-76
3-11-76
3-12-76
3-13-76
3-14-76
3-15-76
3-16-76
3-17-76
3-18-76
3-19-76
3-20-76
3-21-76
3-22-76
3-23-76
3-24-76
3-25-76
3-26-76
3-27-76
3-28-76
3-29-76
3-30-76
24.OC
C.O
42 .00
0.0
0.0
50.00
3400.
3400.
8500.
0.1020E 05
0.1020E 05
6800.
0.1020E 05
0.1700E 05
0.1870E 05
8500.
8500.
0.2380E C5
0.1190E 05
6800.
0.ie70E 05
0.1360E 05
5. 200
5. 800
4.600
4. 400
4.800
4. 800
4.400
4.000
3. 800
4. 600
4. 000
76.00
75.00
86 .00
86.00
87.00
83.00
77.00
85.00
8 4.00
86.00
60.00
5.400
5.300
5.200
5.400
5.300
5.300
5.300
5.300
5.500
5.300
.947
.965
.591
, 884
.965
4. C4 9
4. 879
b. 597
3. 884
3. 8C6
4. 049
4.531
.325
.641
. 426
.398
.225
. 172
.440
.440
, 524
.806
. 799
, 799
.172
2.607
2.758
3.021
4.426
2. 799
2. 799
2.973
2.840
3.021
3.460
3. 806
2.572
3.120
2.883
3. 120
2.928
3.281
3.731
2. 572
2.883
7.813
5.20b
4. 717
5. 102
5. 208
5.319
6.410
7.353
5. 102
5. OOC
5.319
5. 952
5.682
6. 098
5. 814
4.464
4.237
4.167
3. 205
3.205
4. 630
5.000
3. 6 76
3.676
4.167
3.425
3.623
, 96 0
.814
.6 76
.676
.906
. 731
. 968
. 545
.000
3.378
4. 0^8
3. 788
4.098
3. 846
4.310
4.902
3.376
3. 7es
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGI: 3 OF 9
PART 4 OF 6
04/06/77
DATE
25
DIG SUPT
SET SCJLIDS
(ML/L)
26
FECAL
COL I FORM
(ORG./100)
27
SLUDGE
HAULED
(GAL.)
2b
P.C. TOTAL
SOL. SLDGE
HAULEO
29
PERCENT
VOLAT I L E
SOLiDS
30
PH OF
SLUDGE
HAULED
31
DET. TIME
NEW PRIM.
CLAR (HRS»
32
DET. TIME
OLD PRIM.
CLAR < H R SI
3-31-76
4- 1-76
4- 2-76
4- 3-76
4- 4-76
4- 5-76
4- 6-76
4- 7-76
4- 0-76
4- 9-76
4-10-76
4-11-76
4-12-76
4-13-76
4-14-76
4-15-76
4-16-76
4-17-76
4-18-76
4-19-76
4-20-76
4-21-76
4-22-76
4-23-76
4-24-76
4-25-76
4-26-76
4-2 7-76
4-28-76
4-29-76
4-30-76
5- 1-76
5- 2-76
5- 3-76
5- 4-76
5- 5-76
5- 6-76
5- 7-76
5- 8-76
5- 9-76
5-10-76
5-11-76
5-12-76
5-13-76
5-14-76
0.0
22.00
0.0
58.00
2.C0C
13. OC
0.1020E 05
3400.
G.1150E 05
0.1360E 05
1700.
0.1020E 05
C.1190E 05
0.1360E 05
0.1530E 05
0.1020E 05
5100.
1700.
6800.
0.1360E 05
0.1190E 05
0.1360E 05
0.1360E 05
0.1190E 05
0.1360E 05
0.1360E 05
3400.
8500.
3.400
4. 200
4.200
4.200
3.200
3.600
3. 800
4.400
3.600
3.400
85.00
80.00
80.00
87.00
83.00
78.00
86.00
63.00
e8.eo
5.300
5.400
5.400
5.400
5.500
5.300
5.200
5. 300
5.400
5.400
2.138
3.225
2.840
3. 398
3.460
2.64 3
2.680
2. 799
2.719
2.719
3. 1 72
3. 591
2. 758
2.758
2.8e 3
2. 758
3.281
3.225
3. 884
2.643
2.680
2.973
2.758
3.021
3.591
3.660
2.799
2. 640
3.021
2.758
2. 840
3.069
3. 806
2.719
2.840
2.883
2.840
3.069
3. 731
3.591
2.680
2.643
2.643
3.C69
2.928
2. 809
4.237
3. 731
4. 4 64
4 ¦ 5 4 5
3.47^
3. 521
3.676
3.571
3.571
4. 16 T
4.71?
3. 623
3. 62 3
3. 788
3.623
4.310
4.237
5. 102
3.472
3. 521
3. 906
3. 623
3.968
4.717
4.006
3 . 6 71>
3. 731
3. 960
3. 623
3. 731
4.032
5. 000
3. 571
3.731
3.780
3. 731
4. 032
4.902
4.717
3. 521
3.472
3.4 72
4. 032
3.846
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT PAGE 4 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PARI 4 OF b
DATA TABLE
04/06/77
DATE
25
DIG SUPT
SET SOLIDS
(ML/LI
26
FECAL
COL I FOR M
(ORG./100 I
27
SLUDGE
HAULED
(GAL.(
28
P.C. TOTAL
SOL. SLDGE
HAULED
29
PERCENT
VOLAT I L E
SOLIDS
30
PH OF
SLUDGE
HAULED
31
DET. TIME
NEW PRIM.
CLAR (HRS)
32
DET. TIME
OLD PRIM.
CLAR (HRS)
5-15-76
-
-
-
-
-
-
3.460
4 - 545
5-16-76
-
-
-
-
-
-
3.460
4.545
5-17-76
-
-
-
-
-
-
2.607
3.425
5-18-76
-
-
-
-
-
-
2.758
3.623
5-19-76
_
7 . COG
-
-
-
-
2. 840
3.731
5-20-76
-
-
-
-
-
-
2.719
3.571
5-21-76
-
-
-
-
-
-
3.021
3.968
5-22-76
-
-
-
-
-
-
3.591
4.717
5-23-76
-
-
-
-
-
-
3. 806
5.C00
5-24-76
-
-
0.1 190E
05
3.600
83.00
5.200
2.758
3.623
5-25-76
-
8- COC
C.1360E
05
3.400
76.00
5.200
2.504
3.289
5-26-76
-
-
5100.
-
-
-
2.799
3. 676
5-27-76
-
-
6 8 C 0.
-
-
-
3.120
4. 09d
5-28-76
-
-
0.1360E
05
-
-
-
3.225
4.237
5-29-76
_
-
-
-
-
-
3.731
4. 902
5-30-76
-
-
-
-
-
-
4.325
5.682
5-31-76
-
-
-
-
-
-
4. 137
5.435
6- 1-76
-
©
o
-
-
-
-
2.572
3.376
6- 2-76
-
-
-
-
-
-
2.840
3. 731
6- 3-76
-
_
-
-
-
-
2.758
3.623
6 - A 76
-
-
-
-
-
-
3.069
4.032
6- 5-76
_
-
-
-
-
-
3.398
4 . 464
6- 6-76
-
-
-
-
-
-
4. 137
5,435
6- 7-76
-
-
-
-
-
-
3.069
4.03^
6- 8-76
-
-
85 CO.
-
-
-
2. 928
3. 84b
6- 9-76
-
23. OC
0.1190E
05
3.400
82.00
5.300
3.069
4.032
6-10-76
-
-
0.1190E
05
-
-
-
3.069
4.032
6-11-76
-
-
-
-
-
-
2.607
3.425
6-12-76
-
-
-
-
-
-
3.281
4.310
6-13-76
-
-
-
-
-
-
3.660
4. 808
6-14-76
-
o
o
0.1190E
05
3.600
77.00
5.400
2.680
3.521
6-15-76
-
-
0.1190E
05
3.200
75.00
5.300
2.572
3.376
6-16-76
-
-
C.1350E
05
-
-
-
2.504
3.2 89
6-17-76
-
-
-
-
-
-
2.504
3.289
6-1B-76
-
-
-
-
-
-
2.719
3.571
6-19-76
-
-
-
-
-
-
3.660
4. 808
6-20-76
_
-
-
-
-
-
3.460
4.545
6-21-76
_
_
-
-
-
2.471
3.247
6-22-76
_
_
_
-
-
-
2.643
3.472
6-23-76
-
-
-
-
_
-
2.928
3. 046
6-24-76
-
40.OC
-
-
-
-
2.680
3.521
6-25-76
300.0
-
-
-
-
-
3.281
4. 310
6-26-76
_
_
-
-
-
-
3. 731
4.902
6-27-76
-
_
-
-
-
-
3.965
5.203
6-28-76
-
16.OC
68CC.
-
-
-
2. 504
3.289
f> i -r ¦¦ i <
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - lc/31/76
DATA TABLE
PAGE 5 OF
PART 4 OF
9
6
04/06/77
DATE
25
DIG SUPT
SET SOLIDS
(ML/L I
26
FECAL
COL I FORM
(ORG./100)
27
SLUDGE
HAULED
(GAL.I
28
P.O. TOTAL
SOL. SLDGE
HAULED
29
PERCENT
VOL AT ILE
SOL IDS
30
PH OF
SLUOGE
HAULED
31
DET. TIME
NEW PRIM.
CLAR (HRS1
32
DET. TIME
OLD PRIM.
CLAP (MRS)
6-29-76
6-30-76
7- 1-76
7- 2-76
7- 3-76
7- 4-7&
7- 5-76
7- 6-76
7- 7-76
7- 8-76
7- 9-76
7-10-76
7-11-76
7-12-76
7-13-76
7-14-76
7-15-76
7-16-76
7-17-76
7-18-76
7-19-76
7-20-76
7-21-76
7-22-76
7-23-76
7-24-76
7-25-76
7-26-76
7-27-76
7-28-76
7-29-76
7-30-76
7-31-76
8- 1-76
8- 2-76
8- 3-76
8- 4-76
8- 5-76
8- 6-76
8- 7-76
8- 8-76
b- 9-76
8-10-76
8-11-76
8-12-76
8500.
28. OC
0.0
69.00
0.0
0.0
1000.
3000.
0.1100E 05
O.HCOE 05
9000.
1000.
7000.
80CC.
9000.
10000.
C.UOCE 05
10000.
3. 400
76.00
5.600
3.600
3.600
3.400
3.400
3. 800
72.00
66.00
76.00
76.00
75.00
6.000
6.000
6.200
6.300
200 .0
3000.
2.607
2. 840
2.660
2.973
3. 591
4.531
3. 398
2.440
2.409
2.643
2.680=
2. 883
3.8C6
2.471
2.719
2.719
2.719
2.680
3.281
3.731
2.680
2.537
2.572
3. 069.
2.607
3.281
3. 524
2.643
2.719
2.719
2.349
3. 120
4.229
4.641
2.680
2.471
3.225
2.643
2.4C9
2.758
3.C6S
2.471
2.440
2.680
2.537
3.425
3.731
3. 521
3. 906
4.717
5. 952
4.464
3. 205
3. 165
3.472
3.521
3. 786
000
247
571
571
571
521
4.310
4. 902
3.521
3.333
3. 370
4. 032
3.425
4.310
4.630
3.472
3.571
3. 571
3.086
4. 098
5. 556
6. 098
3. 521
3.247
4.237
3.472
3.165
3. 623
4. C32
3.247
3.205
3. 521
3.333
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 6 OF
PART 4 OF
9
6
04/06/77
DATE
25
DIG SUPT
SET SOLIDS
(HL/L )
21
FECAL
COL I FORM
(ORG./100)
27
SLODGE
HAULED
(GAL . I
28
P.C. TOTAL
SOL. SLDGE
HAULED
29
PERCENT
VOLATILE
SOLIDS
30
PH OF
SLUDGE
HAULED
31
DET. TIME
NEW PRIM.
CLAR (HRSI
32
DET. TIME
OLD PRIM.
CLAP (HRSI
8-13-
8-14-
8-15-
8-16-
8-17-
8-18-
8-19-
8-20-
8-21-
8-22-
0-23-
8-24-
8-25-
8-26-
8-27-
8-28-
8-29-
6-30-
8-31-
9- 1-
9-
9-
9-
9-
9-
9-
9- 8-
9- 9-
9-10-
9-11-
9-12-
9-13-
9-14-
9-15-
9-16-
9-17-
9-18-
9-19-
9-20-
9-21-
9-22-
9-23-
9-24-
9-25-
9-26-
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
0.0
0.0
198.0
C.O
190.0
7GC0.
10000.
6000.
0.1200E 05
0.1100E 05
9000.
3000.
1C000.
0.1200E 05
9COO.
8000.
8CC0.
9000.
0.1600E 05
0.1440E 05
0.1430E 05
0.1300E 05
5.400
4.800
5.000
4.600
4.600
4. 800
3.800
4.600
3.400
3.800
4.600
70.00
71.00
68 .00
65.00
65.00
66.00
63.00
65.00
70.00
57.00
60.00
6. 800
6.800
6.800
6.600
6.800
6.800
7.000
7.000
6.800
6.700
6.700
6.700
6.600
80.00
80.00
2.680
3.460
3. 524
2. 572
3. 021
2.440
2. 758
2.572
3.591
3. 731
2. 321
2. 928
2.680
2.607
2.719
3.731
3. 731
2. 5C4
2.6eo
2.799
2. 799
2.719
3.965
4.137
3.591
2.607
2.799
2.719
2.758
3. 8C6
3. 524
2.6C7
3. 660
2. 799
1.487
2. 5C4
3.460
4. 049
2.321
2.471
2.293
2.643
2. 799
3.884
4.049
3. 521
4. 545
4.630
3.378
. 968
, 205
,623
.378
.717
. 902
, 04 9
84 6
.521
.42?
!71
4.902
4.902
3. 289
3. 521
3.676
3. 67b
3.571
5.208
5.435
4.717
3.425
3.676
3.571
3. 623
5. 000
4.630
3.425
4. 806
3.676
1.953
3. 289
4. 545
5. 319
3.049
3.247
3.012
3.472
3.676
5. 102
5.319
-------
NEW HOLLAND t PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01776 - 12/31/76
DATA TABLE
PAGE 7 OF
P4PT 4 OF
9
6
04/06/77
DATE
25
DIG SUPT
SET SOLIDS
< ML/L )
26
FECAL
COL I FORM
(ORG./100 I
27
SLLDGE
HAULED
(GAL.I
28
P.C. TOTAL
SOL. SLDGE
HAULED
29
PERCENT
VOLATIL E
SOLIDS
30
PH OF
SLUDGE
HAULED
31
DET. TIME
NEW PRIM.
CLAR (hRSI
32
DEI. II ME
OLD PRIM.
CLAP (HRSI
9-27-76
150.0
-
-
-
-
-
2.680
3.521
9-28-76
120.0
-
-
-
-
-
3.069
4. 032
9-29-76
160 .0
28.00
0.1300E 05
4.800
66.00
6.700
3.120
4.098
9-30-76
-
-
-
-
-
_
2.440
3.205
10- 1-76
-
-
-
-
-
-
-
-
10- 2-76
-
-
-
-
-
-
10- 3-76
_
-
_
-
-
-
2.440
3.205
10- 4-76
150.0
-
-
-
-
-
2. 504
3.289
10- 5-76
160 .0
-
-
-
-
-
2.607
3.425
10- 6-76
160 .0
-
-
-
-
-
2.799
3. 676
10- 7-76
-
0.0
-
-
-
-
2.607
3.425
10- 8-76
170.0
-
-
-
-
-
2.471
3. 247
10- 9-76
_
-
-
-
-
-
2.572
3.378
10-10-76
-
-
-
-
-
-
3.225
4.237
10-11-76
150.0
-
-
-
-
-
2.537
3.333
10-12-76
-
0.0
1300.
-
-
-
2.643
3.472
10-13-76
130.0
-
-
-
-
-
3.021
3.968
10-14-76
-
-
-
-
-
-
2.640
3. 731
10-15-76
_
-
-
-
-
-
2.799
3.676
10-16-76
-
-
-
-
-
-
3.731
4.902
10-17-76
-
-
-
-
-
-
4.229
5. 556
10-18-76
200 .0
-
-
-
-
-
2.758
3. 623
10-19-76
-
-
0.1300E 05
-
-
-
2.660
3.521
10-20-76
-
-
-
-
-
-
1.962
2.577
10-21-76
-
22.OC
-
-
-
-
2.471
3.247
10-22-76
150.0
-
-
-
-
-
2. 840
3. 731
10-23-76
-
-
-
-
-
-
3.460
4.545
1G-24-76
_
-
-
-
-
-
3.172
4.167
10-25-76
130 .0
-
-
-
-
-
2.504
3.289
10-26-76
130.0
-
-
-
-
-
2.265
2.976
10-27-76
130 .0
-
-
-
-
-
2.643
3.472
10-28-76
130.0
0.0
260C.
-
-
-
2.799
3.676
10-29-76
150 .0
-
2600.
-
-
-
2.719
3.571
10-30-76
-
-
-
-
-
-
3.339
4. 386
10-31-76
-
-
-
-
-
-
3.339
4. 386
11- 1-76
-
-
2600.
5.400
57-00
6.800
2. 572
3.378
11- 2-76
_
-
5200.
-
-
-
2.840
3.731
11- 3-76
_
0.0
9100.
-
-
-
2.973
3. 906
11- 4-76
_
-
-
-
-
-
2.758
3.623
11- 5-76
80.00
-
-
-
-
-
2.840
3. 731
11- 6-76
-
-
-
-
-
-
-
11- 7-76
-
-
-
-
-
-
-
-
11- 8-76
85.00
5.00C
-
-
-
-
2. 799
3.6 76
11- 9-76
80.00
-
-
-
-
-
3. 120
4.098
11-10-76
-
-
9100.
-
-
-
3. 172
4.167
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
page 8 OF 9
PART A OF 6
04/06/77
DATE
25
DIG SUPT
SET SOL I OS
(ML/L )
26
FECAL
COL IFORM
(ORG./100»
27
SLUOGE
HAoLED
(GAL.)
28
P.C. TOTAL
SOL. SLOGE
HAULED
29
PERCENT
VOLATIL E
SOL IDS
30
PH OF
SLUDGE
HAULED
31
OET. TIME
NEW PRIM.
CLAR (HPS)
32
DET. II ME
OLD PRIM.
CLAP (HRSI
11-11-76
11-12-76
11-13-76
11-14-76
11-15-76
11-16-76
11-17-76
11-18-76
11-19-76
11-20-76
11-21-76
11-22-76
11-23-76
11-24-76
11-25-76
11-26-76
11-27-76
11-26-76
11-29-76
11-30-76
12- 1-76
12- 2-76
12- 3-76
12- 4-76
12- 5-76
12- 6-76
12 7-76
12- 8-76
12- 9-76
12-10-76
12-11-76
12-12-76
12-13-76
12-14-76
12-15-76
12-16-76
12-17-76
12-18-76
12-19-76
12-20-76
12-21-76
12-22-76
12-23-76
12-24-76
12-25-76
0.0
15.OC
3.C0C
39.00
0.0
1300.
0.1170E C5
9100.
9100.
0.1300E 05
1300.
5200.
0.1300E 05
0.104OE 05
65CC.
0.1300E
65 CO.
3400.
6500.
6500.
52 C 0.
05
4.000
3.000
2.800
3.400
3.00C
2.400
65.00
73.00
71.00
76.00
80.00
83 .00
6 .600
6.300
6.400
6.400
6.400
6.300
2. 973
3.225
.884
.806
¦ 021
.758
.928
. 799
2.660
3.172
3.591
2. 643
2.799
2. 504
3.281
3.281
3.225
3. 591
2.719
3.C69
2.926
2. 758
2.840
.922
. 504
. 4 C 9
.213
.719
2. 643
2.607
3.281
3.120
2.680
2. 680
2. 799
2.840
2.471
3.591
3.660 '
2.68C
2.680
2. 840
2.928
2.928
4.137
3. 906
4.23 7
5. 1 02
5. COO
3. 968
3. 623
3. 846
3.676
3. 521
4. 167
4.717
3.4 72
3. 6 76
3. 289
4. 310
4.310
4.237
4.717
3.571
4. C32
3. 846
.623
. 731
.525
.289
.165
, 907
3. 571
3.472
3.425
4.310
4. 098
3.521
3. 521
3.676
3. 731
3.247
4.717
4. 808
3. 521
3. 521
3. 731
3. 846
3. 846
5. 435
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 9 OF 9
PAPT 4 OF 6
04/06/77
DATE
25
DIG SUPT
SET SOLIDS
(ML/L )
2 f
FECAL
COL I FOR M
(ORG./ICC)
27
SLUDGE
HAULED
(GAL.)
28
P.C. TOTAL
SOL. SLOGE
HAULED
29
PERCENT
VOLATILE
SOL IDS
30
PH OF
SLUDGE
HAULED
31
DET. TIME
NEW PRIM.
CLAR (HPS)
32
DEI. TIME
OLO PRIM.
CLAP (HRS)
12-26-76
12-27-76
12-28-76
12-29-76
12-30-76
12-31-76
35.00
23.00
24.00
63.00
2.883
2.719
2.799
2.928
2.471
3. 788
3. 571
3.676
3. 846
3.247
MINIMUM
MAXIMUM
AVERAGE
STD.DEV.
VLD.PTS.
2.000
300 .0
97. 17
75. 16
35
0.0
24C0 .
6. 406
348. 2
49
10C0.
0.2380E 05
9168.
4338.
110
2.400
5.800
4.093
0.7835
54
57 .00
88.00
75.57
8.205
53
5.2C0
7.000
5.953
0 .6628
51
1.106
5.947
3.072
0.6431
361
1.453
7. 813
4. 036
0.6449
361
NOr E - ( I SEE FOOTNOTE TABLE.
* SEE COMMENT TABLE.
T,G,L, OR 0 = TRACE, GREATER THAN, LESS THAN, OR QUESTIONABLE DATA.
-------
NEW HOLLAND
OATE
33
DET. T IME
FINAL CLAR
( HRS )
34
O.F. RATE
NEW P CLAR
(GPD/S.F.I
35
O.F. RATE
OLD P CLAR
(GPD/S.F.)
1- 1-76
4.015
481. C
755.5
1- 2-76
3.957
488. 1
766.7
1- 3-76
3.792
509. 3
800.0
1- 4-76
4 .789
403. 2
633.3
1- 5-76
3.957
488. 1
766.7
1- 6-76
3.900
495. 2
777.8
1- 7-76
4.136
466. 9
733.3
1- 8-76
3.845
502. 3
788.9
1- 9-76
4.075
474.0
744.4
1-10-76
5 .460
353. 7
555.5
1-11-76
4.8/5
396. 1
622.2
1-12-76
3.792
509. 3
8OC.0
1-13-76
3.329
580. 1
911.1
1-14-76
4.0 15
481. 0
755.5
1-15-76
4.015
481. 0
755.5
1-16-76
3.845
502.3
788.9
1-17-76
5.056
382. C
600.0
J-18-76
4.875
396. 1
622.2
1-19-76
1.596
1210.
1900.
1-20-76
1.587
1217.
1911.
1-21-76
4.075
474. C
744.4
1-22-76
3.792
509. 3
800.0
1-23-76
4.0 15
481. 0
755.5
1-24-76
4.789
403.2
633.3
1-25-76
4.789
403.2
633.3
1-26-76
4.200
459. 8
722.2
1-27-76
2.528
764. C
1200.
1-28-76
4.403
438. 6
688.9
1-29-76
4.875
396. 1
622.2
1-30-76.
4.0 15
481.0
755.5
1-31-76
8.273
233. 4
366.7
2- 1-76
4 .789
403. 2
633.3
2- 2-76
4.875
396. 1
622.2
2- 3-76
5.0 56
382. C
60 C. 0
2- 4-76
4 . 5 50
424. 4
666.7
2- 5-76
7.378
261. 7
411.1
2- 6-76
4.475
431. 5
677.8
2- 7-76
7.000
275. 9
433.3
2- 8-76
8.27 3
233.4
366.7
2- 9-76
5.460
353. 7
555.5
2-10-76
5.2 50
367. 6
57 7.8
2-11-76
5.607
339. 6
533.3
2-12-76
5 .353
360. e
566.7
2-13-76
5.250
367. e
577.8
2-14-76
7.8 00
247. t
388.9
I o;; i
PA WASTEWATER TREATMENT PLANT
REPORT u I/O 1/76 - 12/31/76
DATA TABLE
PAGi; 1 OF 9
PART 5 OF 6
04/06/77
36
O.F. RATE
FINAL CLAR
(GPD/S.F.)
37
WEIR LOAD.
OLD P CLAR
(GPD/FT.)
38
WEIR LOAD.
NEW P CLAR
(GPD/FT.I
39
WEIR LOAD.
FINAL CLAR
(GPD/F T.)
40
HYD. LOAD.
TRICK FILT
MG/A/DAY
346. 3
0.2264E
05
3611 .
4332.
3.237
351.4
0 .22986
05
3664.
4395.
3.284
366.7
0.2398 E
05
3823.
45e6.
3.427
290.3
0. 1898E
05
3027 .
3631.
2. 713
35 1.4
0.2298E
05
3664 .
4395.
3.284
356.5
0.2331E
05
3717.'
4459.
3.332
336.1
0.2198E
05
3505.
4204.
3. 142
361.6
0 .2364 E
05
3770.
4523.
3.380
341.2
0.2231E
05
3558.
4268.
3. 189
254.6
0 . 1665E
05
2655.
3185.
2.380
285.2
0. 1865E
05
2974.
3567.
2.666
366.7
0.2398E
05
3823.
4586.
3.427
417.6
0.27 31E
05
4354.
5223.
3.903
346.3
0.2264E
05
3611 .
4332.
3.237
346.3
0 .2264 E
05
3611.
4332.
3.237
361.6
0.2364E
05
3770.
4523.
3.380
275.0
0.1798E
05
2867 .
3440.
2.570
285.2
0. 1865E
05
2974.
3567.
2.666
870.9
0.5694E
05
9080.
0.1089E
05
8.140
876.0
0.57^8 E
C'5
9133.
0.1096E
05
0.187
341.2
0.2231E
05
3558.
4268.
3.189
366.7
0.2398E
05
3823.
4586.
3.427
346.3
0.2264E
05
361 1 .
4332.
3.237
290.3
0. 1098E
05
3027.
3631.
2.713
290.3
0.1898E
05
3027.
3631.
2.713
33 1.0
0 . 2 164 E
05
345 1 .
4 140.
3.094
550.0
0.3596 E
05
5735.
6880.
5.141
315.8
0.2065 E
05
3292.
3949.
2.951
285.2
0. 1865E
05
2974.
3567.
2 666
346.3
0.2264E
05
3611.
4332.
3.237
168.1
0.1099E
05
1752 .
2102.
1.571
290.3
0. 1898E
05
3027.
3631.
2.713
285.2
0.1865E
05
2974.
3567.
2.6 66
275.C
0.1798E
05
2867 .
3440.
2.570
305.6
0.199b E
05
3186.
3822.
2. 856
188.4
0.1232 E
05
1965.
2357.
1.761
310.7
0.203 1E
05
3239.
2886.
2.904
198.6
0.1299E
05
207 1.
2464.
1.856
168.1
0. 1099E
05
1752.
2102.
1.571
254.6
0 . 1665E
05
2655.
3185.
2.380
264.8
0.1732E
05
2761.
3312.
2.475
244. 5
0 . 1598 E
05
2549 .
305e.
2.285
259.7
0. 1698 E
05
2708.
3249.
2.428
264.8
0.1732E
05
2761.
3312.
2.475
178.3
0.1165L
05
1858.
2229.
1.666
-------
NEW HOLLANO. PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGF 2 OF 9
PART 5 OP 6
04/06/77
DATE
33
OET. TIME
FINAL CLAR
( HRS )
34
O.F. RATE
NEW P CLAR
(GPD/S.F.I
35
O.F. RATE
OLD P CLAR
(GPD/S.F.)
3b
O.F. RATE
FINAL CLAR
(GPD/S.F.)
37
WEIK LOAD.
OLD P CLAR
(GPD/FT.1
38
WEIR LOAD.
NEW P CLAR
(GPD/FT.)
39
WEIR LOAD.
FINAL CLAR
(GPD/F T.)
'.0
HYD. LOAD.
TFICK P1LT
MG/A/DAY
2-15-76
8.531
2-16-76
5 .687
2-17-76
5. 1 51
2-1876
5.571
2-19-76
5.687
2-20-76
5 .809
2-21-76
7.000
2-22-76
8.029
2-23-76
5.571
2-24-76
5 .460
2-25- 16
5.809
2-26-76
6.500
2-27-76
6.205
2-28-76
6.659
2-29-76
6.349
3- 1-76
4.875
3- 2-76
4.627
3- 3-76
4.5 50
3- 4-76
3.500
3- 5-76
3.500
3- 6-76
5.056
3- 7-76
5.460
3- 8-76
4.0 15
3- 9-76
4.0 15
3-10-76
4.5 50
3-11-76
3.740
3-12-76
3.957
3-13-76
4.333
3-14-76
6.349
3-15-76
4.015
3-16-76
4.015
3-17-76
4.266
3-18-76
4.075
3-19-76
4.333
3-20-76
4.964
3-21-76
5.460
3-22-76
3.689
3-23-76
4.475
3-24-76
4. 136
3-25-76
4.475
3-26-76
4.200
3-27-76
4 .707
3-28-76
5.3 53
3-29-76
3.6 89
3-30-76
4.136
226. 4
339.6
374. 9
346. 6
339.6
332. 5
275.9
240. S
34 6. 6
353. 7
332. 5
297. 1
311. 3
290.C
304. 2
396. 1
417. 4
424. 4
551. e
551. 8
382. 0
353. 7
461.0
481. 0
424. 4
516.4
488. 1
445. 7
304. 2
481. C
481. 0
452. 7
474. 0
445. 7
389. 1
353. 7
523. 5
431. 5
466. 9
431. 5
459. 6
410. 3
360. 8
523. 5
466.9
355.6
163.0
O.IO06E
05
1699.
2038.
1.523
533.3
244.5
0.1598E
05
2549 .
3058.
2.285
588.9
269.9
0.1765E
05
2814.
3376.
2. 523
54 4.4
249.6
0 .1632E
05
2602.
3121.
2.332
533.3
244.5
0.1598E
05
2549.
3058.
2.285
522.2
239.4
0.1565E
05
2496 .
2994.
2.237
433.3
198.6
0. 1299E
05
207 1.
2484.
1. 856
377.8
173.2
0.1132E
05
1805.
2166.
1.618
544.4
249.6
0. 1632E
05
2602.
3121.
2. 332
555.5
2 54.6
0. 1665E
05
2655.
3185.
2. 380
522.2
239.4
C . 15o5E
05
2496.
2994.
2.237
466.7
213.9
0.1399E
05
2230.
2675.
1.999
488.9
224. 1
0.1465 E
05
2336.
2803.
2. 09't
455.6
208.8
0. 1365E
05
2177 .
2612.
1.952
477.8
219.0
0 .1432E
05
2283.
2739.
2. 04 7
622.2
285.2
0.1865E
05
2974.
3567.
2. 666
655.5
300.5
0.1965G
05
3133.
3758.
2.808
66 6.7
305.6
0.1998E
05
3186.
3822.
2. 656
066.7
397.3
0.2597E
05
4142.
4969.
3.713
866.7
397.3
' 0.2597E
05
4142.
4969.
3.713
600.0
275.0
O.1790E
05
2867.
3440.
2. 570
555.5
254.6
0.16&5E
05
2655.
3185.
2.380
755.5
346.3
0 .2264 E
05
3611.
4332.
3.237
755.5
346.3
0.22 64 E
05
3611.
4332.
3.237
666.7
305.6
0.199GE
05
3186 .
3822.
2. 856
811.1
371.8
0.2431E
05
3876.
4650.
3.475
76 6.7
35 1.4
0.2298E
05
3664
4395.
3.28^
700.0
320.9
0.2098 E
05
3345.
4013.
2.999
477.8
219.0
0.1432E
05
2283.
2739.
2.047
755.5
346.3
0.2 264E
05
3611.
4332.
3.23?
755.5
346.3
0.2264 E
05
3611.
4332.
3.237
711.1
326.0
0.2131E
05
3398.
4077.
3. 046
744.4
34 1.2
0.2231E
05
3558.
4268.
3. 189
700.0
32 0.9
0 .2098 E
05
3345.
401 3.
2. 999
611.1
280. 1
0.1831E
05
2920.
3503.
2.618
555.5
254.6
0.1665E
05
2655.
3185.
2.380
822.2
376.9
0.2464E
05
3929.
471^.
3.522
67 7.8
310.7
0.2031E
05
3239.
3886.
2. 904
733.3
336.1
0.2198E
05
3505.
4204 .
3. 142
677.8
310.7
0.20 J1 fc
05
3239.
3886.
2. 904
722.2
331.0
0.2lC4 E
05
345 1 .
4 140.
3. 094
644.4
295.4
0.I931E
05
3080 .
3695.
2.761
56 6.7
259.7
0.1698 E
05
2708 .
3249.
2.426
822.2
376.9
0.2 464 E
05
3929.
4714.
3.522
733.3
336. 1
0.2198E
05
3505.
4204.
3. 142
-------
76
76
¦ 7 6
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
76
NEW HOLLAND, PA WASTEWATER TREATMENT PI ANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
04/06/77
33
DET. TIME
FINAL CLAR
( HRS »
34
U.F. RATE
NEW P CLAR
(GPD/S.F.)
35
O.F. P.ATE
OLD P CLAR
(GPD/S.F.)
36
O.F. RATE
FINAL CLAR
(GPD/S.F.)
37
WEIR LOAD.
OLD P CLAR
(GPD/FT.)
38
WEIR LOAD.
NEW P CLAR
(GPD/FT.)
39
WEIR LOAD.
FINAL CLAR
(GPD/FT.)
3.067
629. 6
988.9
453.3
0.29 64E
05
4726.
5669.
4.627
417.4
655.5
300.5
0. 1965E
05
3133.
3758.
4.075
474. C
744.4
341.2
0.2231E
05
3558.
4268.
4.675
396. 1
622.2
285.2
0. 1865E
05
2974.
3567.
4 .964
389. 1
611.1
280. 1
0. 1831E
05
2920.
3503.
3.792
50 S. 3
8CO.O
366 7
0.2398E
05
3823.
4586.
3. 845
502. 3
> 788.9
361.6
0.2 364 E
05
3770.
4523.
4.015
481. 0
755.5
34 6.3
0 .2 264 E
05
3611.
4332.
3.900
495. 2
777.8
356.5
0.2 33 I E
05
37 17.
4459.
3.900
495. 2
777.8
356.5
0.2331e
05
3717.
4459.
4.5 50
424. 4
666.7
305.6
0.1998E
05
3186.
3822.
5.151
374. 9
588.9
269.9
0.1765E
05
2814.
3376.
3.957
486. 1
766.7
351.4
0.2296 E
05
36b4.
4395.
3.957
488. 1
76 6.7
351.4
0.2 298 E
05
3664.
4395.
4. 136
44>fc S
733.3
336. 1
0.2198E
05
3505.
4204.
3.9 57
488. 1
766.7
351.4
0.C298E
05
3664.
4395.
4 .707
410. 3
644.4
295.4
0.19 31E
05
3080.
3695.
4.627
417.4
655.5
300.5
0.1965E
05
3133.
3 75 G.
5.571
346.6
544.4
249.6
0 . 1632E
05
2602.
3121.
3.792
509.3
80C.0
366.7
0 .2 390 E
05
3823.
4586.
3 .845
502. 3
788.9
361.6
0 . 2 364 E
05
3770.
4 523.
4.266
452. 7
711.1
326.0
0.2131E
05
3 398.
4077.
3.957
488. 1
766.7
351.4
0 .2298E
05
3664 .
4395.
4.333
445. 7
700.0
320.9
0.2098E
05
334 5. ¦
4013.
5. 151
374.9
588.9
269.9
0.1765E
05
2814.
3376.
5.2 50
367. e
577.8
264. 8
0.1732E
05
2761.
3312.
4.0 15
481.0
755.5
346.3
0 2264 E
05
3611.
4332.
4.075
474. C
744.4
341.2
0.2231E
05
3558.
4268.
4.3 33
445. 7
70C.0
320.9
0.2098E
05
3345.
4013.
3.957
488. 1
766.7
351.4
0 .2298E
05
36c>4.
4395.
4.075
474. C
744.4
341.2
0 .2231E
05
3558.
4268.
4.403
438.6
68e.9
315.8
0.2065E
05
3292.
3949.
5 .460
353. 7
555.5
254.6
0.1665 E
05
2655.
3185.
3.900
495. 2
777.8
356.5
0.2331E
05
3717.
4459.
4.075
474. 0
744.4
341.2
0.2231E
05
3558.
426B.
4 . 136
466. 9
733.3
336.1
0.2198E
05
3505.
4204.
4.075
474. C
744.4
34 1.2
0 .2231 E
05
3558.
4268.
4.403
438. t
688.9
315.8
0 . 2065 E
05
3292.
394S.
5.353
360. e
566.7
259.7
0.1698E
05
2708.
3249.
5.151
374.9
586.9
269.9
0.1765 E
05
2814.
3376.
3.845
502. 3
788.9
361.6
0.2364 E
05
3770.
4523.
3. 792
509. 3
800.0
366.7
0.2 398E
05
3823.
4586.
3 .792
509. 3
800.0
366 . 7
0 .2398E
05
3823.
4586.
4.403
438. e
688.9
315.8
C .2065E
05
3292.
3949.
4.200
459. e
722.2
331.0
0.2164 E
05
3451.
4140.
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 4 OF 9
PART 5 OF 6
04/06/77
DATE
33
OET . TIME
FINAL CLAR
( HRS )
34
O.F. RATE
NEH P CLAR
JGPD/S.F.)
35
O.F. RATE
OLD P CLAR
(GFO/S.F.)
36
O.F. RATE
FINAL CLAR
(GPD/S.F.)
37
WEIR LOAD.
OLD P CLAR
(GPD/FT. )
38
WEIR LOAD.
NEW P CLAR
(GPD/FT.)
39
WEIR LOAD.
F 1NAL CLAR
(GPO/FT.I
'.0
HYD. LOAD.
TRICK FILT
MG/A/DAY
5-15-76
4.9 64
5-16-76
4 .964
5-17-76
3.740
5-18-76
3.957
5-19-76
4.075
5-20-76
3.900
5-21-76
4 .333
5-22-76
5.151
5-23-76
5.460
5-24-76
3.957
5-25-76
3.592
5-26-76
4.015
5-27-76
4 .4 75
5-28-76
4.627
5-29-76
5.3 53
5-30-76
6.205
5-31-76
5.935
6- 1-76
3.689
6- 2-76
4.075
6- 3-76
3.957
6- 4-76
4.403
6- 5-76
4.875
6- 6-76
5.935
6- 7-76
4.403
6- 8--76
4.200
6- 9-76
4.403
6-10-76
4.403
6-11-76
3.740
6-12-76
4.707
6-13-76
5.2 50
6-14-76
3.845
6-15-76
3.6 89
6-16-76
3 .592
6-17-76
3.592
6-16-76
3.900
6-19-76
5.2 50
6-20-76
4.964
6-21-76
3.545
6-22-76
3.792
6-23-76
4.200
6-24-76
3.845
6-25-76
4.707
6-26-76
5.353
6-27-76
5 .687
6-28-76
3.592
389. 1
389. 1
516.4
488. 1
474. 0
495. 2
445. 7
374. S
353. 1
488.1
537.6
481. C
431.5
417.4
360. e
311. 3
325.4
523. 5
474. 0
488. 1
438. t
396. 1
325.4
438. 6
459. e
438. t
438. t
516.4
410. 3
367. e
502. 3
523. 5
537. £
537.6
495. 2
367. 6
3 8 9. 1
544. 7
£05.3
459. e
502. 3
410. 3
36C. e
339.6
537. 6
611.1
280.1
0.1831E
05
2920.
3503.
2.618
611.1
280. 1
0. 1831R
05
2920.
3503.
2. 610
011.1
371.8
0.2431E
05
3876 .
465C.
3.475
766.7
351.4
0 .229BE
05
3664.
4395.
3.2 84
744.4
341.2
0.2 231E
05
3558.
4268.
3. 189
777.8
356.5
0 . 331 E
05
3717.
4459.
3.332
700.0
320.9
0.2098E
05
3345.
4013.
2. 999
588.9
269.9
0.1765E
05
2814.
3376.
2. 523
555.5
254.6
0. 1665 E
05
2655.
3185.
2.380
766.7
351.4
0.2298E
05
3664
4395.
3.284
844.4
307.1
0.2531E
05
4036.
4841.
3.618
755.5
346.3
0.2264E
05
3611.
4332.
3 . 2 ?7
677.8
310.7
0.2031E
05
3239 .
3886.
2.904
655.5
300.5
0. 1965E
05
3133.
3758.
2. 808
566.7
259.7
0.1698E
05
2708.
3249.
2.428
488.9
224.1
0.1465 E
05
2336.
2803.
2.094
511.1
234.3
0.1532E
05
2443.
2930.
2.190
822.2
376.9
0 . 2464E
05
3929.
4714.
3. 522
744.4
341.2
0.2231E
05
3558.
4268.
3. 189
766.7
351.4
0.2 298 E
05
3664.
4395.
3.2 84
688.9
315.8
0.2065E
05
3292.
3949.
2.951
622.2
285.2
0.1865E
05
2974.
3567.
2.666
511.1
234.3
0.1532E
05
2443.
2930.
2. 190
688.9
315.8
0.2065E
05
3292.
3949.
2.951
722.2
331.0
0.2164E
05
3451.
4140.
3. 094
688.9
315.8
0 .2065E
05
3292.
3949.
2.951
68e.9
315.8
0.2065E
05
3292.
3949.
2.951
811.1
371.8
0.2431E
05
3876.
465C.
3.475
644.4
295.4
C.1931E
05
3080.
3695.
2.761
577.8
264.8
0 . 1 732 E
05
2761.
3312.
2.475
788.9
36 1.6
0.2364 E
05
3770.
4523.
3.380
822.2
376.9
C .2 464E
05
3929 .
4714.
3. 522
84 4.4
387.1
0.2531E
05
4036.
4841.
3.618
844.4
387.1
0.2531E
05
4036.
4841.
3.618
777.8
356.5
0.2331E
05
3717.
. 4459.
3.332
577.8
264.6
0.1732E
05
2761.
3312.
2.475
611.1
280. 1
0.1831E
05
2920.
3503.
2. 618
855.5
392.2
0 .2564E
05
4089.
4905.
3.665
800.0
366.7
0.2398 E
05
3823.
4586.
3.427
722.2
331.0
0.c164 E
05
345 1.
4140.
3.094
788.9
361.6
0.2364E
05
3770.
4523.
3.380
64 .4
295.4
0.1931E
05
3080.
3695.
2. 761
566.7
259.7
0.169BE
05
2708.
3249.
2.428
533.3
24 4.5
C. 1598F
05
25-.9.
3058.
2.285
844.4
387. 1
0.2531E
05
4036.
4841.
3.618
-------
NEW HOLLAND
DAT E
6-29-76
6-30-76
7- 1-76
7- 2-76
7- 3-76
7- 4-76
7- 5-76
7- 6-76
7- 7-76
7- 8-76
7- 9-76
7-10-76
7-11-76
7-12-76
7-13-76
7-14-76
7-15-76
7-16-76
7-17-76
7-18-76
7-19-76
7-20-76
7-21-76
7-2 2-76
7-23-76
7-24-76
7-25-76
7-26-76
f-27-76
7-26-76
7-29-76
7-30-76
7-31-76
8- 1-76
8- 2-76
8- 3-76
8- 4-76
8- 5-76
8- 6-76
8- 7-76
8- 8-76
8- 9-76
8-10-76
8-11-76
8-12-76
33
OET TIME
FINAL CLAR
( HRS )
3 4
O.F. RATE
NEW P CLAR
C GPD/S.F.I
35
O.F. RATE
OLD P CLAP.
(GPD/S.F.I
3 .740
4.075
3.845
4 .266
5.151
6.500
4.875
3.500
3.456
3.792
3.845
4 .136
5 .460
3.545
3.900
3 .900
3.900
3.845
4.707
5.353
3.845
3.640
3.689
4 .403
3.740
4.707
5.0 56
3.792
3.900
3.900
3.370
4.475
6.067
6.6 59
3.845
3.545
4.627
3.792
3.456
3.957
4.403
3.545
3.500
3 .845
3 .640
51 fc. 4
474.0
502. 3
452. 7
374. S
297. 1
396. 1
55 1. 8
558. 8
509.3
502. 3
466. S
353. 7
544. 7
495. 2
495. 2
495. 2
502. 3
410. 3
360. 8
502.3
530. 5
523. 5
438. t
516.4
410. 3
382. 0
509.3
495. 2
495. 2
573. C
431. 5
318.3
290. 0
502. 3
544. 7
417.4
509. 3
558. 8
486. 1
438. t
544. 7
551. 8
502. 3
530. 5
811.1
744.4
788.9
711.1
588.9
466.7
622.2
866.7
877.8
80C.0
786.9
733.3
555.5
865.5
77 7.8
777.8
77 7.8
788.9
644.4
566.7
788.9
833.3
822.2
668.9
811.1
644.4
600.0
800.0
777.8
777.8
900.0
677.8
50C.0
455.6
788.9
855.5
655.5
800.0
877.8
76 6.7
688.9
855.5
666.7
78ti.9
833.3
PA WASTEWATER TREATMENT PLANT
REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 5 OF 9
PAP.T 5 OF 6
04/06/77
36
C.F. RATE
FINAL CLAR
(GPD/S.F.)
37
WEIR LOAD.
OLD P CLAR
(GPD/FT.)
38
WEIR LOAD.
NEW P CLAR
(GPD/FT.I
39
WEIR LOAD.
FINAL CLAR
(GPD/FT. I
4 0
HYD. LCAD.
TPICK FILT
MG/A/DAY
371.8
0.24 31E
05
341.2
0.2231E
05
361.6
0.2364 E
05
326.0
0 . £ 1 311
05
269.9
0.1765E
05
213.9
C.1399E
05
285.2
0.1865E
05
397.3
0.2 597 E
05
402.3
0.2631E
05
366.7
0.2398E
05
361.6
0.2364E
05
336. 1
0.2198E
05
254.6
0. 1665E
05
392.2
0.2 564 E
05
356.5
0.2331E
05
356.5
0.2331E
05
356.5
0.2 331E
05
361.6
0.2364E
05
295.4
0.1931E
05
259.7
0. 1698E
05
361.6
0.2364E
05
382.0
0.2498E
05
376.9
0.2464E
05
315.8
0.20 65 E
05
371.8
0.2431b
05
295.4
0. 1931E
05
275.0
0. 1798E
05
366.7
0.2396E
05
356.5
0.2331E
05
356.5
0.2 331E
05
412.5
0.2697E
05
310.7
0 . 203 1 E
05
229.2
0.1498E
05
208.8
0. 1365 E
05
361.6
0.2 364 E
05
392.2
0.2 564 E
05
300.5
0.1965E
05
366.7
0.2398E
05
402.3
0.2631E
05
35 1.4
0.2298E
05
315.8
0.2065E
05
392.2
0.2 564 E
05
397.3
0.2597E
0 5
361.6
0.236*» E
05
382.0
0.2 498E
05
3876.
3558.
3770.
3398.
2814 .
2230.
2974.
4142.
4195.
3823.
3770.
3505.
2655.
4089.
3717.
3717.
3717.
3770.
3080.
2708.
3770.
3983.
3929.
3292.
3876.
3080.
2 867.
3823.
3717.
3f 17.
4301 .
3239 .
2389.
2177.
3770.
4089.
3133.
3823.
4195.
3664 .
3292 .
4089.
4142.
3770.
3983.
4650.
4268.
4523.
4077.
3376.
2675.
3567.
4969.
5032.
4586.
4523.
4204.
3185.
4905.
4 459.
4459.
4459.
4523.
3695.
3249.
4 5 2 3.
4778.
4714.
3949.
4650.
3695.
344C.
4586.
4459.
4459.
5160.
3886.
2866.
2612.
452?.
4905.
3758.
4586.
5032.
4395.
3949.
4905.
4969.
4523.
4 7 78.
475
189
300
046
523
999
666
3.713
3. 760
3.427
3. 380
3.142
2.380
3.665
3.332
3.332
3. 332
3.380
2.761
2.428
3.380
3. 5 70
3.522
2.951
3.475
2. 761
2. 570
3. 427
3. 332
3.332
3. 656
2.904
2.142
1. 952
3. 380
3.665
2. 808
3.427
3. 760
3.284
2.951
3. 665
3. 713
3. 380
3.570
-------
NEW HOLLAND
DATE
8-13-76
8-14-7b
8-15-76
8-16-76
6-17-76
8-18-76
8-19-76
8-20-r6
8-21-76
8-22-76
8-23-76
8-24-76
8-25-76
8-26-76
8-27-76
b-2 8-76
8-29-76
8-30-76
8-31-76
9- 1-76
9- 2-76
9- 3-76
9- 4-76
9- 5-76
9- 6-76
9- 7-76
9- 8-76
9- 9-76
9-10-76
9-11-76
9-12-76
9-13-76
9-14-76
9-15-76
9-16-76
9-17-76
9-18-76
9-19-76
9-20-76
9-21-76
9-22-76
9-23-76
9-24-76
9-25-76
9-26-76
33
OET . T IME
FINAL CLAR
( HRS I
34
O.F. RATE
NEW P CLAP
(GPD/S.F.)
35
O.F . RATE
OLD P CLAR
(GPD/S.F.I
3.845
4-964
5.0 56
3.6 89
4.3 33
3 .500
3.957
3.689
5. 1 51
5.353
3.3 29
4.200
3.845
3.7 40
3.9 00
5.353
5.353
3.592
3.845
4.0 15
4.0 15
3 ,900
5.687
5.9 35
5. 151
3 .740
4.015
3.900
3.957
5.460
5.0 56
3 .740
5.2 50
4 .0 15
2.1 33
3.592
4 .9 64
5 .809
3.329
3.545
3. 289
3.792
4.015
5.571
5.8 09
502. 3
389. 1
382. C
523.5
44 5.7
551. e
488. 1
523. 5
374. 9
360. e
580. 1
459. 8
502. 3
516. 4
495. 2
360. e
360. 8
537.6
502. 3
481. 0
481. C
49 5. 2
339. fc
325.4
374.9
516.4
481. C
495. 2
488. 1
353. 7
382. C
516.4
367. e
481.0
905. 5
537. 6
309. 1
332. 5
580. I
544. 7
587. 1
509. 3
481.0
346.6
332.5
783.9
611.1
600.0
822.2
700.0
866.7
766.7
822.2
588.9
566 7
911.1
722.2
788.9
811.1
777.8
566.7
566. 7
844.4
780.9
755.5
755.5
777.8
533.3
511.1
588.9
811.1
755.5
777.8
766.7
555.5
600.0
81 1.1
577.8
755.5
1422.
844.4
611.1
522.2
911.1
855.5
922.2
600.0
755.5
544.4
522.2
PA WASTEWATER TREATMENT PLANT
REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 6 OF 9
PART 5 OF 6
04/06/77
36
O.F. RATE
FINAL CLAR
(GPD/S.F.I
37
WEIR LOAD.
OLD P CLAR
( GPD/FT . )
3e
WEIR LOAD.
NEW P CLAR
(GPD/FT.)
39
WEIR LOAD.
FINAL CLAR
(GPD/FT.)
40
HYD. LOAD.
TRICK FILT
MC/A/DAY
361.6
280.1
275.0
376.9
320.9
397.3
351.4
376.9
269.9
259.7
417.6
331.0
36 1 .6
371.8
356.5
259.7
259.7
387.1
361.6
346.3
346.3
356.5
244.5
234.3
269.9
371.8
346.3
356.5
3^1.4
254.6
275.0
371. 8
264.8
346.3
651.9
387.
280.
239.
417.
392.
422.
366.
346.
249.6
239.4
2 364 E 05
I831E 05
1 798 E 05
2464 E 05
2090E 05
2 59 7 E 05
0.2298E 05
0.Z464E 05
0.1765E 05
0.1698E 05
0.2731E 05
0.2164E 05
0.2 364 E 05
0.2431E 05
0.2331E 05
0.1698E 05
0.1698 E 05
0.2531E 05
0.2364E 05
0.2264E 05
0.2264E 05
0.2331E 05
0.1598E 05
0.1532E 05
0.1765E 05
0.2431E 05
0.2264E 05
0.2331E 05
0.2298E 05
1665E 05
1798 E 05
2431 E 05
1732E 05
2 2 64 E 05
4262E 05
2531 E 05
1831E 05
1565E 05
2 7 31 E 05
2564 E 05
2 764 E 05
2398E 05
2264E
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0.1632E 05
0.1565E 05
05
3770.
2920.
2867.
3929.
3345 .
4142.
3664.
3929 .
2814 .
2708.
4 3 5 4.
3451.
3770.
3876.
3717.
2708.
2706.
4036.
3770.
3611.
361 1.
3717.
2549 .
2443.
2814 .
3876.
3611.
3717.
3664.
2655.
2867.
3876.
2761 .
3611.
6797.
4036.
2920.
2496.
4354 .
4089 .
4407.
3823.
361 1.
2602.
2496.
4523.
3503.
3440.
4714.
4013.
4969.
4395.
4 714.
3376.
3249.
5223.
4 140.
4523.
465C.
4459.
3249.
3249.
4841.
4523.
4332.
4332.
4459.
305e.
293C.
3376.
4650.
4332.
4459.
4395.
3185.
3440.
4650.
3312.
4332.
8154.
4841.
3503.
2994.
5223.
4905.
5287.
4586.
4332.
3121.
2994.
3.380
2.618
2.570
3.522
2. 999
3.713
3.2 04
3.522
2.523
2.420
3. 903
3.094
3. 360
3.475
3.332
2.428
2. 428
3.618
.3 80
.237
.237
.332
.285
. 190
2.523
3.475
3.237
3 .332
3.284
2.380
2.570
3.475
2.475
3.237
6. 093
3.618
2.618
2.237
3.903
3.665
3. 951
3.427
3.23 I
2.332
2.237
-------
NEW HOLLAND
DATE
33
OET. TIME
FINAL CLAR
( MRS )
3
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 8 OF 9
PART 5 OF 6
04/06/77
DATE
33
DET. TIME
FINAL CLAR
( HRS »
34
O.F. RATE
NEW P CLAR
(GPD/S.F.»
35
O.F. RATE
OLD P CLAR
(GPD/S.F.)
36
O.F. RATE
FINAL CLAR
(GPD/S.F.I
37
WEIR LOAD.
OLD P CLAR
(GPD/FT.I
38
WEIR LOAD.
NEW P CLAR
< GPD/FT.)
3<3
WEIR LOAD.
FINAL CLAR
IGPD/FT.I
40
HYD. LOAD.
TRICK FlLT
MG/A/DAY
11-11-76
4.266
452. 7
711.1
326.0
0 .2131E
05
3398.
4077.
3.046
11-12-76
4.627
417.4
655.5
300.5
0. 1965E
05
3133.
3758.
2. 808
11-13-76
5. 571
346. t
544.4
249.6
0 . 1632E
05
2602.
3121.
2. 332
11-14-76
5.460
353. 7
555.5
254.6
0.1665 E
05
2655.
3185.
2.380
11-15-76
4.333
44 5. 7
700.0
320.9
0.2098E
05
3345.
4013.
2.999
11-16-76
3.957
488. 1
766.7
351.4
0.229&E
05
3664.
4395.
3.284
11-17-76
4.2 00
459. 8
722.2
33 1 .0
0.2164E
05
3451.
4140.
3.094
11-18-76
4.0 15
481. 0
755.5
346.3
0.2264E
05
3611.
4332.
3.237
11-19-76
3.845
502. 3
788.9
361.6
0.23t.4E
05
3770.
4523.
3.380
11-20-76
4.550
424.4
666.7
305.6
0 . 1998E
05
3186.
3822.
2. 8 56
11-21-76
5. 151
374. 9
588.9
269. 9
0 . 1 765E
05
2814.
3376.
2. 523
11-22-76
3.792
509. 3
800.0
366.7
0 .2398 E
05
38 23.
4586.
3.427
11-23-76
4.015
481.C
755.5
346.3
0.2264E
05
3611.
4332.
3.237
11-24-76
3.592
537.6
844.4
387. 1
0.2531E
05
4036.
4841.
3.618
11-25-76
4.707
410. 3
644.4
295.4
0. 1931E
05
3080.
3695.
2.761
11-2 6-7b
4.707
410. 3
644.4
295.4
0 . 19 31 E
05
3080.
3695.
2.761
11-27-76
4.6 27
417.4
655.5
300.5
019 65 £
05
3133.
3758.
2. 808
11-28-76
5. 151
374. 9
588.9
269.9
0.1765E
05
2814.
3 3 76.
2. 523
11-29-76
3.900
495. 2
777.8
356.5
0.2331E
05
3717.
4459.
3.332
11-30-76
4.403
438. 6
688.9
315.8
0.2065E
05
3292.
3949.
2.951
12- 1-76
4.200
459.8
722.2
331.0
0.2164E
05
3451.
4140.
3.094
12- 2-76
3.9 57
488. 1
766.7
351.4
0 .2298E
05
3664.
4395.
3.204
12- 3-76
4.075
474. C
744.4
341.2
0.2231E
05
3558 .
4268.
3. 189
12- 4-76
2.7 58
700.3
1100.
504.2
0 .3297E
05
5257.
6306.
4. 712
12- 5-76
3.592
537. t
844.4
387. 1
0.2531E
05
4036.
4841.
3.618
12- 6-76
3.4 56
55e. e
877.8
402.3
0.2631E
05
4195.
5032.
3. 760
12- 7-76
3. 174
608.4
955.5
438.0
0.2864E
05
4567.
5478.
4.094
12- 8-76
3.900
495. 2
777.8
356.5
0.2331E
05
3717.
44 59.
3. 332
12- 9-76
3.792
509. 3
800.0
366.7
0.2398E
05
3823 .
4586.
3.427
12-10-76
3.740
516.4
811.1
371.8
0.2431E
05
3876.
4650.
3. 475
12-11-76
4.707
410. 3
644.4
295.4
0. 1931E
05
3080.
3695.
2. 761
12-12-76
4.475
431. 5
677.8
310.7
0.2031E
05
3239.
3886.
2.904
12-13-76
3.845
502. 3
788.9
361.6
0 .2364 E
05
3770.
4523.
3. 380
12-14-76
3.845
502. 3
788.9
361.6
0.2364 E
05
3770.
4523.
3.380
12-15-76
4.015
481. 0
755.5
346.3
0.2264E
05
3611.
4332.
3.237
12-16-76
4.075
474. 0
744.4
341.2
0 . 2 2 31 fc
05
3558.
4268.
3.189
12-17-76
3.545
544 7
855.5
392.2
0.2564E
05
4089.
4905.
3. 665
12-18-76
5.151
374.9
588.9
269.9
0.1765E
05
2814.
3376.
2. 523
12-19-76
5.2 50
367. e
577.8
264.8
0. 1732E
05
2761.
3312.
2.475
12-20-76
3.845
502. 3
788.9
361.6
0.2364E
05
3770.
4523.
3. 380
12-21-76
3.845
502. 3
788.9
361.6
0 . 2364E
05
3770.
4523.
3.380
12-22-76
4.075
474. 0
744.4
341.2
0 .2231E
05
3558.
4268.
3. 189
12-23-76
4.200
459. e
722.2
331.0
0 . 2164 E
05
3451.
4140.
3.094
12-24-76
4.200
459. 8
722.2
331.0
0.2164E
05
3451.
4140.
3.09
-------
IMEVJ HOLLAND» PA WASTEWATER TREATMENT PLANT PAt,E 9 Of 9
OPERATING PEPORT 01/01/76 - 12/31/76 PARI 5 G f- 6
OATA TAbLE
04/06/77
OATE
33
OET. TIME
FINAL CLAR
( HRS )
34
O.F. RATE
NEW P CLAP.
650
361
NOTE - < > StE FOOTNOTE TABLE.
* S':E COMMENT TABLE.
T.G.L, OR 0 = TRACE. GREATER THAN, LESS THANt OR QUESTIONABLE DAI A.
-------
NEW HOLLAND, PA WAS T EWAT Efi T fl E AT MENT PL AM
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
04/06/77
41
ORG LOADNG
TF LB BOD/
DATE 1000 C.F.
1- 1-76
1- 2-76
1- 3-76
1- 4-76
1- 5-76
1- 6-76
1- 7-76
1- 8-76 8 .0 30
1- 9-76
1-10-76
1-11-76
1-12-76
1-13-76
1-14-76 14.45
1-15-76
1-16-76
1-17-76
1-18-76
1-19-76
1-20-76
1-21-76
1-22-76 16.99
1-23-76
1-24-76
1-25-76
1-26-76
1-27-76
1-28-76
1-29-76
1-30-76 17.11
1-31-76
2- 1-76
2- 2-76
2- 3-76
2- 4-76
2- 5-76
2- 6-76
2- 7-76 8.936
2- 8-76
2- 9-76
2-10-76
2-11-76 11.28
2-12-76
2-13-76
2-14-76
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT PAGE 2 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 6 OF 6
DATA TABLE
04/06/77
41
ORG LOADNG
TF LB BOD/
OATE 1000 C.F.
2-15-76
2-16-76
2-17-76
2-18-76
2-19-76
2-20-76
2-21-76
2-22-76
2-23-76 11.47
2-24-76
2-25-76
2-26-76
2-27-76
2-26-76
2-29-76
3- 1-76
3- 2-76
3- 3-76
3- 4-76
3- 5-76
3- 6-76
3- 7-76
3- 8-76
3- 9-76
3-10-76
3-11-76
3-12-76
3-13-76
3-14-76
3-15-76
3-16-76
3-17-76
3-18-76
3-19-76
3-20-76
3-21-76
3-22-76
3-23-76
3-24-76
3-25-76
3-26-76 16.35
3-27-76
3-28-76
3-29-76
3-30-76
: ? >' (?
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 3 OF 9
PART 6 OF 6
41
ORG LOADNG
TF LB BOD/
DATE 1000 C.F.
3-31-76
4- 1-76 11.33
4- 2-76
4- 3-76
4- 4-76 -
4- 5-76
4- 6-76
4- 7-76
4- 0-76 16.86
4- 9-76
4-10-76
4-11-76
4-12-76
4-13-76
4-14-76 14.93
4-15-76
4-16-76
4-17-76
4-18-76
4-19-76
4-20-76
4-21-76
4-22-76 10.70
4-23-76
4-24-76
4-25-76 '
4-26-76
4-27-76
4-28-76
4-29-76 6.795
4-30-76
5- 1-76
5- 2-76
5- 3-76
5- 4-76
5- 5-76
5- fc-76 20.25
5- 7-76
5- 0-76
5- 9-76
5-10-76
5-11-76
5-12-76 16.15
5-13-76
5-14-76
04/06/77
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT PAGE 4 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 6 OF 6
DATA TABLE
04/06/77
41
ORG LOADNG
TF LB BOD/
DATE 1000 C.F.
5-15-76
51676 -
5-17-76
5-18-76
5-19-76 31.03
5-20-76
5-21-76
5-22-76
5-23-76
5-24-76
5-26-76
5-26-76
5-27-76 8.743
5-28-76
5-29-76
5-30-76
5-31-76
6- 1-76
6- 2-76 11.43
6- 3-76
6- 4-76
6- 5-76
6 6-76
6- 7-76
6- 8-76
6- 9-76
6-10-76 8.644
6-11-76
6-12-76
6-13-76
6-14-76
6-15-76
6-1676 36.16
6-17-76
6-18-76
6-19-76
6-20-76
b-21-76
6-22-76
6-23-76
6-24-76
6-25-76 6.843
6-26-76
6-27-76
6-28-76
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT PAGE 5 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 6 OF 6
DATA TABLE
04/06/77
41
ORG LOADNG
TF LB BOO/
OATE 1000 C.F.
6-29-76
6-30-76 14.50
7- 1-76
7- 2-76
7- 3-76
7- 4-76
7- 5-76
7- 6-76
7- 7-76
7- 8-76
7- 9-76 14.68
7-10-76
7-11-76
7-12-76
7-13-76
7-14-76
7-15-76
7-16-76
7-17-76
7-1G-76
7-19-76
7-20-76
7-Z1-76
7-22-76
7-23-76 34.95
7-24-76
7-25-76
7-26-76
7-27-76
7-28-76
7-29-76
7-30-76 10.59
7-31-76
8- 1-76
8- 2-76
8- 3-76
8- 4-76
8- 5-76
8- 6-76 11.55
8- 7-76
8- 8-76
8- 9-76
8-10-76
8-11-76
8-12-76
-------
NE In HOLLAND, PA WASTEHATER TfttATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
DATA TABLE
PAGE 6 OF 9
PART 6 OF 6
04/06/77
OATE
41
ORG LOADNG
TF LB BOD/
1000 C.F.
8-13-76 11.01
8-14-76
8-15-76
8-16-76
8-17-76
8-18-76
8-19-76
8-20-76 20.13
8-21-76
8-22-76
8-23-76
8-24-76
8-25-76
8-26-76
8-27-76 6.211
8-28-76
8-29-76
8-30-76
8-31-76
9- 1-76
9- 2-76
9- 3-76 26.89
9- 4-76
9- 5-76
9- 6-76
9- 7-76
9- 8-76
9- 9-76
9-10-76 10.83
9-11-76
9-12-76
9-13-76
9-14-76
9-15-76
9-16-76
9-17-76 20.75
9-18-76
9-19-76
9-20-76
9-21-76
9-22-76
9-23-76
9-24-76 22.01
9-25-76
9-26-76
-------
NEW HOLLAND, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/0L/76 - 12/31/76
DATA TABLE
PAGE
PART
7 OF
6 OF
9
6
04/06/77
41
ORG LOADNG
TF LB BOD/
DATE 1000 C.F.
9-27-76
9-28-76
9-29-76
9-30-76
10- 1-76
10- 2-76
10- 3-76
10- 4-76
10- 5-76
10- 6-76
10- 7-76
10- 8-76 15.69
10- 9-76
10-10-76
10-11-76
10-12-76
10-13-76
10-14-76
10-15-76
10-16-76
10-17-76
10-18-76
10-19-76
10-20-76
10-21-76
10-22-76 24.89
10-23-76
10-24-76
10-25-76
10-26-76
10-27-76
10-28-76
10-29-76 24.3/
10-30-76
10-31-76
U- 1-76
11- 2-76
11- 3-76
11- 4-76
11- 5-76 32.40
11- 6-76
11- 7-76
11- 8-76
11- 9-76
11-10-7&
-------
NEW HOLLAND. PA WASTEWATER TREATMENT PLANT PAGE 8 OF 9
OPERATING REPORT 01/01/76 - 12/31/76 PART 6 OF 6
DATA TABLE
04/06/77
41
ORG LOADNG
TF LB BOD/
DATE 1000 C.F.
11-11-76
11-12-76
11-13-76
11-14-76
11-15-76
11-16-76
11-17-76
11-18-76
11-19-76
11-20-76
11-21-76
11-22-76
11-23-76
11-24-76
11-25-76
11-26-76
11-27-76
11-28-76
11-29-76
11-30-76
12- 1-76
12- 2-76
12- 3-76
12- 4-76
12- 5-76
12- 6-76
12- 7-76
12- 8-76
12- 9-76
12-10-76
12-11-76
12-12-76
12-13-76
12-14-76
12-15-76
12-16-76
12-17-76
12-18-76
12-19-76
12-20-76
12-21-76
12-22-76 27.96
12-23-76
12-24-76
12-25-76
-------
NEW HOLLANO, PA WASTEWATER TREATMENT PLANT
OPERATING REPORT 01/01/76 - 12/31/76
OATA TABLE
PAGE 9 OF 9
PART 6 OF 6
04/06/77
41
ORG LOAONG
TF LB BOO/
DATE 1000 C.F.
12-26-76
12-27-76
12-28-76
12-29-76
12-30-76 46.47
12-31-76
MINIMUM 6.211
MAXIMUM 46.47
AVERAGE 17.44
STO.OEV. 9.349
VLD.PTS. 39
NOTE - ( ) SEE FOOTNOTE TABLE.
* SEE COMMENT TABLE.
TtG.Li OR 0 = TRACE, GREATER THAN, LESS THAN, OR QUESTIONABLE OATA.
-------
APPENDIX D
-------
APPEND I X I)
LABORATORY TESTING CAPABILITY AND PERFORMANCE
WASTEWATER TREATMENT FACILITY
N1:W HOLLAND, PENNSYLVANIA
Parameter
Flow
BODr
Suspended Solids
Fecal Coll form
Phosphorus
Anunonia Nitrogen
Nitrate Nitrogen
Total Kjeldahl
Dissolved Oxygen
Chlorine Residual
COD
Capability
Yes
Yes
Yes
Yes
Yes
Yes
Yes
Testing Method
Parshal1 Flume
11.0. Meter
Millipore
pi I Meter
Dissolved Oxygen
Meter
Orthotolodine
Frequency
Cont i niious
1/week
Da i 1 y
Week]y
DaJ 1 y
Dai ly
Daily
Sampling Location
Inf1uent
Influent, Effluent
Influent, Effluent
Ef f 1uent
Raw, Primary ClarifrLcr,
Effluent, Secondary Ef-
fluent, Final Effluent
Type of Sample (1)
G
Trickling Filter Effluent, G
Final Effluent
Final Effluent G
Other
(1) C-8 = Composite, 8-liour
G = Grab
-------
APPENDIX E
-------
AITI.NMX I:
STAFFING ESTIMATE FOR MUNICIPAL WASTEWATER TREATMENT
FACILITY ACCORDING TO EPA
U&M PROCEDURE
, MARCH
1973
, CONTRACT
-01-0328.
BOROUGH OF NEW
HOLLAND WASTEWATER TREATMENT PLANT
DESIGN FLOW 1.000 MGD
I. A 0J US TMfc NT FOR LOCAL CONDITIONS (TABULATED VALUES
ARE ADDED TO
OBTAIN OVERALL PERCENTAGE
ADJUSTMENT
TO TABLE II TOT ALS1
i pr ai rnwni tiiim r nWMPMT
AT,.HIS fMFNT. . .
Lut LUtmUI 1 ID <4 L. U1
OPERAT ION
;1A I NTtNANCE
SUPERVISORY
CLERICAL
LABOR AT OR Y
YAROW'JRK
°LANT LAYOUT AVERAGE
0
0
0
0
0
0
UNIT PROCESSES S T D. E QP , DI F. MANF
0
0
0
0
0
0
LEVEL OF TPEAIMENT SECGNDAPY
0
0
0
0
0
0
1Y°E OF WASTE KEMUVAL REQUIREMENT AMT WASTE IN EPF
10
10
0
0
0
0
INDUSTRIAL WASTE ERRATIC
LO
0
0
0
10
0
n RO DUC TI V ITY OF LABOR AVG. (6.5 HR/DAY)
0
0
0
0
0
0
CLIMATE MODERATE WINTERS
0
0
0
0
0
0
TRAINING CERT S CONTIN.EO
_ q
0
-10
0
0
0
AUIO^ATIC "'ON I TOR I NG MONITORING ONLY
0
0
0
0
0
0
AUTOMATIC SAMPLING NONE
5
0
0
0
5
0
OF^-PLANT LAt3UKA TOR Y WORK NONE
0
0
0
0
0
0
OcF-l'|.ANT '1A IN Tb NANCE NONE
0
0
0
0
0
0
AGE AND CONDITION OF EQUIPMENT OLD/POORLY CARED
0
10
0
0
0
0
PATTFPN Oc NIGHT f. WEEKEND STAFFING STD1/3CAY STA = C
0
0
0
0
0
0
OVERALL ADJUSTMENT
20
20
-10
0
15
0
II. ANNUAL MANHOURS (TABULATED VALUES APPLY UNDER STANDARD CONDITIONS)
MM IT DinCCCC
U 1 r*U'.-02>
OPEP AT ION
MAINTENANCE
SUP ER V ISORY
CLERICAL
LABORATORY
YARDwORK
PU'«P SEWAGE AT PLANT
0
32 7
48
5
30
43
SCR EENING & GRINDING
46
17
9
1
6
B
PRIMARY CLARIFICAT IN
230
215
66
7
41
58
TRICKLING FILTRATION
370
333
104
11
65
91
rRICKG.FILT.CLARIFCN
65
255
47
5
30
42
CIILOR I N AT I ON
128
198
48
5
30
42
ANAEROBIC DIGESTION
190
45
33
3
21
29
TRUCKING
1000
50
155
16
97
137
2019
1440
510
53
320
4 50
ADJUSTMENT (FROM I)
404
280
-50
0
48
0
ADJUSTED TOTAL
2423
1728
460
53
3e>9
450
MI. STAFFING SUGGESTION
OPER AT ION
MA INTENANCE
SUPERVI SOPY
CLERICAL
LABORATORY
YARCWORK
TOTAL MANHOURS PER YEAR
2423
1728
460
53
368
450
NUMBER OF MEN
1.6
1.2
0.3
O.O
0.2
0.3
TOTAL HOURS/YEAR 5482
TOTAL NUMBFR OF HEN 3.7
WEEKDAY- DAY SHIFT 2.1 MEN, NIGHT SHIFT 0.3 MEN, GRAVEYAPD SHIFT 0.3 MEN. WEEKEND- 0.9 HEN..
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