Solid Waste And
Emergency Response
(OS-420) WF
EPA510-R-93-004
July 1993
x>EPA
Cost Guide For
Remediation Equipment
At UST Sites
Printed on Recycled Paper
-------
COST GUIDE
FOR
REMEDIATION EQUIPMENT
AT
UST SITES
JULY 1993
United States Environmental Protection Agency
Office Of Underground Storage Tanks
This manual was prepared for the United States Environmental Protection Agency, Office of Underground Storage
Tanks under Contract Number 68-WO-0024 with ICF Incorporated and its subcontractor, Oataquest Corporation.
Neither the United States Environmental Protection Agency nor any of its employees, contractors, subcontractors,
or their employees makes any warranty, expressed or implied, or assumes any legal liability or responsibility for any
third party's use of or the results of such use of any information, apparatus, product, or process disclosed in this
manual, or represents that its use by such third party would not infringe on privately owned rights.
-------
CONTENTS
Cost Guide for Remediation Equipment
at UST Sites
Section Title Page
1 Introduction 1-1
2 Remediation Equipment 2-1
2 Adsorbers
2 Carbon, Liquid Phase 2-1
2 Carbon, Vapor Phase 2-2
2 Aerators
2 Tray 2-3
2 Packed Tower Air Strippers 2-5
2 Pugmill Mixers 2-6
2 Bins 2-6
2 Oil/Water Separators 2-9
2 Blowers 2-10
2 Conveyors
2 General Purpose Conveyors 2-11
2 Belt Feeders 2-12
2 Vibrating Grizzly Feeders 2-12
2 Apron Feeders 2-14
2 Scalping Screens 2-15
1993
-------
CONTENTS
Cost Guide for Remediation Equipment
at UST Sites
Section Title Page
2 Drum Deheaders 2-15
2 Enhanced Aerators
2 Rototillers
2 Walk-Behind Rototillers 2-15
2 Self-Propelled Ride-On Rototillers 2-16
2 Low Temperature Thermal Desorbers 2-16
2 Soil Vapor Extraction Systems 2-17
2 Dust Collectors
2 Baghouses 2-18
2 Wet Scrubbers 2-19
2 Underground Pipe And Cable Locators 2-19
2 Skimmers 2-19
2 Downhole Filter-Separators 2-20
2 Surface Filter-Separators 2-20
2 Pumps
2 Bladder Pumps 2-20
2 Centrifugal Pumps 2-21
2 Chemical Metering Pumps 2-22
1993
-------
CONTENTS
Cost Guide for Remediation Equipment
at UST Sites
Section Title Page
2 Diaphragm Pumps 2-23
2 Submersible Pumps 2-24
2 Oxidizers
2 Thermal Oxidizers 2-24
2 Catalytic Oxidizers 2-25
2 Fixed Film Bioreactors 2-26
2 Drills
2 Rotary Auger Drills For Truck Mounting 2-26
2 Rotary Auger Drills, Trailer Mounted 2-27
2 Generators
2 Small Generators 2-27
2 Large Generators 2-28
3 Appendices 3-1
3 Appendix A: Rate Adjustment and
Rate Element Tables 3-1
3 Appendix B: Unit Price Information For Materials
Purchased For One Time Use 3-4
3 Appendix C: Chemical Conversion Factors 3-9
1993
-------
CONTENTS
Cost Guide for Remediation Equipment
at UST Sites
Section Title Page
3 Appendix D: Equivalencies
3 D1: Weight And Measure
Equivalencies 3-10
3 D2: Energy Equivalencies 3-12
3 D3: Mechanical-Electrical
Equivalencies 3-12
3 Appendix E: Power Required For Pumping 3-13
3 Appendix F: Variables For Pumping Applications 3-15
4 Glossary 4-1
iv 1993
-------
COST GUIDE
FOR
REMEDIATION EQUIPMENT
AT
UST SITES
JULY 1993
§1. INTRODUCTION
-------
CONTENTS
Section 1. Introduction
Title Page
Introduction 1-1
How This Cost Guide Is Organized 1-1
Rate Structure: Definitions And Methodology 1-2
Ownership Costs 1-2
Operating Costs 1-4
How To Use The Cost Guide 1-4
How To Adjust The Rates In This Cost Guide 1-5
Use The Rate Adjustment Tables To Adjust For Differences In
Age Of Equipment 1-6
Use The Rate Element Tables To Adjust For Standby, Job Severity,
Duplication Of Costs, And Discounts 1-6
Use One Of Two Ways To Adjust For Multiple Shifts 1-8
-------
INTRO DU C TIO N
The Cost Guide for Remediation Equipment at UST Sites provides comprehensive,
current information on the costs for certain equipment (i.e., equipment currently being
manufactured) that is used during the cleanup of petroleum hydrocarbons from soil and
groundwater at the site of a release from an underground storage tank (UST). The
remediation technologies represented in this Cost Guide are influenced significantly by many
site-specific characteristics. Specific contaminant types, containment levels, site geology and
hydrogeology, remediation goals, and many other factors contribute to a fluctuation in actual
costs from one site to another. While Dataquest made significant efforts to ensure total
accuracy, the variable nature of the information and its sources precludes any warranties.
The rates in this Cost Guide represent an average allowance that equipment owners
should charge in order to recoup their ownership and operating costs. Because this manual is
based upon average costs, use discretion in applying the data to evaluate costs at specific sites.
The rates are derived from cost formulas and data developed from research and from analytic
methods used in the equipment industry. Generally, these methods consider purchase price,
depreciation, maintenance and repair costs, indirect equipment costs, and average annual use
hours. Specific market conditions (e.g., local supply and demand) are not considered. These
rates are not a listing of rates being charged nationally by rental companies.1
How This Cost Guide Is Organized
This Cost Guide is divided into four sections: Section 1 is the Introduction, Section 2
contains the Remediation Equipment Tables, Section 3 contains Appendices A through F, and
Section 4 is a Glossary. Pages are numbered by section.
• The Introduction explains how to calculate rate structures, how to adjust rates found
in this Cost Guide, and how to use the Cost Guide. The following three topics are
covered in the remainder of the Introduction:
• Rate Structure: Definitions and Methodology outlines the methodology used
to calculate total, annual, monthly, weekly, and hourly ownership and
operating costs.
• How To Use The Cost Guide describes how the Remediation Equipment
Tables are organized and explains how to use them.
• How To Adjust The Rates In This Cost Guide shows how to use the Rate
Element and Rate Adjustment Tables in Appendix A when calculating
1 The publication of these rates is not intended to influence the rental market of remediation equipment as a
whole. To enter into agreement, combination, understanding, or action with any person or party with intent to
establish rental rates at specific levels in this or any other publication may constitute a violation of Fair Trade
Practices.
1993 §1-1
-------
INTR O D U C TION
adjustments for equipment age and various job elements (e.g., standby, job
severity, duplication of costs, discounts).
The Remediation Equipment Tables outline annual, monthly, weekly, daily, and
hourly ownership costs of specific equipment and systems and include equipment
specifications and performance data where available.
The Appendices supply detailed technical information (e.g., chemical conversion
factors, weight and measure equivalencies) that can be used to compare specifications
or performance data that are otherwise not directly comparable. Other information in
the Appendices (e.g., pumping power requirements) can be useful for selecting
equipment that is appropriate for specific environmental conditions.
The Glossary contains definitions of the technical terms used in this Cost Guide.
Rate Structure: Definitions And Methodology
The rates in this Cost Guide are based on the ownership and operating costs for
contractor-owned equipment. Profit, project overhead, and general company overhead costs
(e.g., office facilities, supplies) are not included.
Ownership Costs
Total ownership costs are the sum of the costs of depreciation, indirect equipment,
facilities capital, and major repair. Each of these costs is explained below.
• The cost of depreciation. In this Cost Guide, "depreciation" means the straight line,
even accrual of funds over the established economic life of a piece of equipment; it
does not refer to any of the other methods of determining depreciation (i.e., for
taxation or other accounting purposes). Depreciation is used to offset the purchase
price.
Depreciation costs are based on the purchase price plus sales tax and original freight
costs minus the cost of a set of new tires (if tire mounted) and minus an allowance for
salvage value at the end of the economic life of a piece of equipment. The purchase
price used in this Cost Guide is the last or most recent manufacturers' suggested list
price available at the time this document was researched. No discount is applied to
this list price.
• The indirect costs of equipment. Allowances are made for indirect costs that result
directly from equipment ownership. These costs include normal risk and liability
insurance, property taxes, storage, licenses, recordkeeping costs, security, and
worker's supervision. Insurance allowance does not include pollution insurance.
§1-2 1993
-------
INT RO D U C TI O N
Indirect costs are sometimes recovered in project or general company overhead. If
any of these costs need to be eliminated from the basic rates in this Cost Guide, refer
to the Rate Element Tables in Appendix A and the accompanying explanation for
these tables in this section under the heading, Use The Rate Element Tables To Adjust
For Standby, Job Severity, Duplication Of Costs, And Discounts.
The cost of facilities capital. The cost of facilities capital (CFC) is an allowance for
the cost of money invested in equipment, whether the equipment is purchased in cash
or financed over time. CFC is not the same as interest charges. CFC is calculated by
using the following formula:
CFC = f(N - H x (1 + S) + 21 x CMR x P
2x N
Where:
N = Economic life of piece of equipment in years
S = Salvage value percentage
CMR = Cost of money rate (as set by the Treasury Department each January 1 and
July 1)
P = Purchase price of the piece of equipment
CFC = Annual cost of facilities capital
The cost of major repair. The ownership rates in this Cost Guide include an
allowance for the major repair costs necessary to keep a piece of equipment functional
throughout its economic life. This allowance covers the periodic rebuilding of major
equipment components.
The life-cycle ownership costs (i.e., depreciation, indirect costs, cost of facilities
capital, and major repair) are annualized and then adjusted to reflect the average
annual working season in order to develop a monthly ownership rate. Weekly, daily,
and hourly rates are derived from the monthly rate. Rates for shorter periods are
increased to account for lost availability and productivity.
The weekly ownership rate is approximately 28 percent of the monthly rate. This
percentage presumes the loss of roughly 32 hours during a month when equipment is
used on a weekly basis.
The daily ownership rate is approximately 25 percent of the weekly rate, based on the
loss of roughly 60 hours during a month when the equipment is used on a daily basis.
The hourly ownership rate is approximately 15 percent of the daily rate, based on the
loss of about 80 hours during a month when the equipment is used on an hourly basis.
1993 §1-3
-------
INTRODUCTION
Operating Costs
Total operating costs are based on the costs of labor and parts, expendables, and
extraordinary expendables. Each of these costs is explained below.
• The cost of labor and parts needed for routine, daily servicing of the equipment.
This includes repairing and/or replacing small components (e.g., pumps, injectors,
filters, gaskets, and worn lines).
• The cost of operating expendables include fuel (computed in accordance with price,
horsepower, and average load factors); lubrications (including filters, oil, and grease);
and tires. Tire costs are calculated by average tire life factors and take into
consideration typical discounts from list prices. Electrical costs are not included.
• The cost of extraordinary operating expendables. The Estimated Operating Cost
per Hour may not include all operating expenses. Ground-engaging components
(e.g., drill bits) are normally excluded because of their highly variable wear patterns,
and operators' wages are not included. These costs should be recovered separately.
How To Use The Cost Guide
Familiarize yourself with both the Contents page (so that you can find the information
you need) and the Introduction (so that you can use the information effectively). Then learn
how this Cost Guide presents information, for example:
Oil/Water Separators
Maximum Capacity
10 gpm
10 gpm
20 gpm
20 gpm
30 gpm
30 gpm
Inlet/Outlet
2.0"
2.0"
2.5"
2.5"
2.5"
2.5"
Oil Outlet
3.0"
3.0"
3.0"
3.0"
3.0"
3.0"
Discharge
Gravity
V, HP Pump
Gravity
1/z HP Pump
Gravity
Vt HP Pump
Gasoline, diesel, air, and electrically powered units are listed separately for some equipment.
Other specifications (e.g., flow rate, dimensions) are given to help identify equipment.
Note the following:
• When horsepower is shown, it is the horsepower used for calculating estimated
operating costs per hour or for identifying variations in like models from the same
§1-4
1993
-------
INTRODUCTION
manufacturer. Whenever possible, flywheel horsepower is used based upon
manufacturers' ratings. For motors, it is 1.341 times the kilowatt rating or as listed
by the manufacturer for a given rpm.
Rates are given by the month, week, day, and hour for each piece of equipment.
Monthly
$115.00
$130.00
$165.00
Weekly
$36.25
$42.00
$52.50
Daily
$10.20
$11.80
$14.70
Hourly
$1.50
$1.75
$2.20
Estimated
Operating
Cost/Hr.
$1.50
$1.90
$2.30
When applicable, the rates should be modified by the Rate Adjustment Table
(Appendix A) factors to reflect a depreciation allowance indexed to the year a piece of
equipment was originally manufactured and sold.
To calculate the total cost for owning and operating a piece of equipment, add the
following items:
• Rental rate for equipment (plus modifications from the Rate Adjustment
Tables when applicable)
• Rate for attachments (when applicable)
• Estimated operating cost
• Operators' wages (including fringe benefits)
• Additional costs for any operating or maintenance personnel who may be
required.
The total cost suggested here is a guideline. It is not meant to define the actual rate
that a lessor may charge. The actual rate may be increased or decreased by factors
not taken into account in this Cost Guide (e.g., severe conditions on the job). Please
note that the operator's wages and additional costs for operating or maintenance
personnel are not included in the cited rates.
How To Adjust The Rates In This Cost Guide
The Rate Adjustment Tables and the Rate Element Tables are in Appendix A.
1993
§1-5
-------
/ N T R O D U C TI O N
Use The Rate Adjustment Tables To Adjust For Differences In Age Of Equipment
Allowances for depreciation costs, which are one of four kinds of ownership costs in
these rates, represent a percentage of the total rate. Depreciation allowances are based on
current or latest price levels for a given piece of equipment. The Rate Adjustment Tables list
depreciation costs according to the year a piece of equipment was originally manufactured.
(When this document was written, analysts used the Producer Price Index, published by the
U.S. Department of Labor, Bureau of Labor Statistics, and manufacturers' price literature to
determine historical and current price levels.) The adjustments ensure that the rates in this
Cost Guide comply with federal cost principles.
The factors in the Rate Adjustment Tables apply only to the basic ownership rates;
they do not apply to the Estimated Operating Cost per Hour or repair costs. The 1993 Rate
Adjustment Tables can only be applied to 1993 rates.
To adjust the rate for a piece of equipment that carries a current model number:
1. Determine the year your piece of equipment was manufactured. (You may need to
refer to an equipment serial number guide.) For example, let's say you have a 500
CFM Thermal Oxidizer manufactured in 1990.
2. Decide which table you should use. There are two tables: Table 1 contains data for
years 1993-1984, and Table 2 contains data for years 1983-1974. Find the rate
adjustment factor for your piece of equipment and the year it was manufactured. For
our example, you would look in Table 1 (because your oxidizer was manufactured in
1990), and you would discover that the factor is .981.
3. Multiply the published rate by the adjustment factor for the year your equipment was
manufactured. In our example,
$1,350 is the monthly published rate for 500 CFM Thermal Oxidizer
x .981 is the adjustment factor for 1990
$1,325 is the adjusted monthly rate for 1990 vintage 500 CFM Thermal Oxidizer
Use The Rate Element Tables To Adjust For Standby, Job Severity, Duplication Of
Costs, And Discounts
The Rate Element Tables (Appendix A) help you adjust the rates for standby, job
severity, duplication of costs, and discounts. The basic rate contains allowances for
depreciation, major repairs, cost of facilities capital (CFC), and indirect equipment costs.
§1-6 1993
-------
INTR O D U C TIO N
The Rate Element Tables show the average percentage of the total rate that each cost
allowance comprises. For example, the tables list the following data for thermal oxidizers.
Equipment
Type
Oxidizers
Depreciation
.40
Major
Overhaul
.14
CFC
.14
Indirect
Costs
.32
Standby rates. A piece of equipment is in a "standby" situation when it is on the job
and available for work but is not put into operation until needed. Under certain
circumstances (e.g., during forced or legal standby), contractors may be entitled to
payments for their equipment on standby. These payments reimburse the contractor
for fixed costs (e.g., depreciation, cost of facilities capital, and indirect equipment
costs).
No industry standard exists for computing standby rates. However, data in the Rate
Element Tables can help users identify an appropriate standby rate. Let's use thermal
oxidizers again. Calculate "standby" for them as follows: Add the factors for
depreciation, cost of facilities capital, and indirect costs to obtain a total percent of the
ownership rate.
.40 = Depreciation
.14 = CFC
+. .32 = Indirect costs
.86(or 86 percent of ownership rate) = Standby rate
The above example is not meant to establish a correct way of determining standby
rates. Determining the specific amounts and cost allowances used in the calculation of
standby rates is the responsibility of the contracting parties.
Job Severity. Rates in this Cost Guide are based on the assumption that equipment is
working mostly under normal job conditions, with occasional light and severe
applications. In some cases, equipment may work consistently in severe job
conditions, which may increase actual repair costs. The Rate Element Tables isolate
the allowance for major repair and adjust it for severity. For example, if severe job
conditions are expected to increase major repair by 10 percent, then you can increase
the ownership rate by adding 10 percent to the repair portion. In the Oxidizer tables,
repair is .14, or 14 percent, of the ownership rate. Multiplying this by 10 percent
gives you 1.4 percent, which is the amount of increase in the total ownership rate.
Remember that prolonged applications in severe job conditions may affect other cost
allowances by decreasing the economic life of a piece of equipment; therefore, other
adjustments may be necessary.
1993
§1-7
-------
INTRODUCTION
Duplication of costs. If costs that are included in the rates are handled through other
procedures, these costs should be deducted from the published rate. For example, if
indirect costs are included in project overhead, then deduct that portion of the
ownership rate. Using the tables for Oxidizers, this means that one would deduct 32
percent from the ownership rate to avoid duplicating the allowance for Indirect Costs.
Discounts. As stated earlier in this Introduction, the ownership rates in this guide do
not include an allowance for a discount from the manufacturer's suggested price. If it
is necessary to account for a discounted purchase price, reduce the depreciation
portion of the ownership rate by an amount equal to the discount percentage. With
Thermal Oxidizers, for example, if the buyer receives a 15 percent discount, reduce
the ownership rate by subtracting 15 percent of 40 percent (the depreciation portion);
in this case, 6 percent.
Use One Of Two Ways To Adjust For Multiple Shifts
Depending on the agreement, you may charge multiple shifts (overtime) in one of the
following ways:
• At l/8th the daily rate for each hour in excess of 8 hours, l/40th of the weekly rate
for each hour in excess of 40 hours, and l/176th of the monthly rate for each hour in
excess of 176 hours within a 30-day period.
• At 150 percent of the base rate for double shifts; 200 percent of the base rate for
triple shifts. For example,
Single shift (8 hours) = $100 per day (base rate)
Double shift (16 hours) = $150 per day
Third shift (24 hours) = $200 per day
§1-8
1993
-------
COST GUIDE
FOR
REMEDIATION EQUIPMENT
AT
UST SITES
§2, REMEDIATION EQUIPMENT
JULY 1993
-------
CONTENTS
Section 2: Remediation Equipment
Title
Adsorbers
Carbon, Liquid Phase
Carbon, Vapor Phase
Aerators
Tray
Packed Tower Air Strippers
Pugmill Mixers
Bins
Oil/Water Separators
Blowers
Conveyors
General Purpose Conveyors
Belt Feeders
Vibrating Grizzly Feeders
Apron Feeders
Scalping Screens
Drum Deheaders
Page
2-1
2-2
2-3
2-5
2-6
2-6
2-9
2-10
2-11
2-12
2-12
2-14
2-15
2-15
1993
§2-i
-------
CONTENTS
Section 2: Remediation Equipment
Title
Enhanced Aerators
Rototillers
Walk-Behind Rototillers
Self-Propelled Ride-On Rototillers
Low Temperature Thermal Desorbers
Soil Vapor Extraction Systems
Dust Collectors
Baghouses
Wet Scrubbers
Underground Pipe And Cable Locators
Skimmers
Downhole Filter-Separators
Surface Filter-Separators
Pumps
Bladder Pumps
Centrifugal Pumps
Chemical Metering Pumps
Diaphragm Pumps
Submersible Pumps
Page
2-15
2-16
2-16
2-17
2-18
2-19
2-19
2-19
2-20
2-20
2-20
2-21
2-22
2-23
2-24
§24
1993
-------
CONTENTS
Section 2: Remediation Equipment
Title Page
Oxidizers
Thermal Oxidizers 2-24
Catalytic Oxidizers 2-25
Fixed Film Bioreactors 2-26
Drills
Rotary Auger Drills For Truck Mounting 2-26
Rotary Auger Drills, Trailer Mounted 2-27
Generators
Small Generators 2-27
Large Generators 2-28
1993
-------
REMEDIATION EQUIPMENT
LIQUID PHASE CARBON ADSORBERS
(All rates include carbon cannister, initial carbon supply, and internal piping. Carbon cannisters are made of steel and internally lined
with an epoxy coating. Pumps, transfer piping, accessory instrumentation, shipping costs, and electricity costs are not included. Rates are
based on one month carbon change-out. Actual carbon life is highly site specific and will vary greatly.)
Height
Manual Povwntd
30 in
40 In
36 in
40 in
40 in
75 in
43 in
46 in
71 In
87 in
72 In
76 in
86 In
86 In
91 In
97 In
112 In
Diameter
20 in
30 in
22 in
26 in
26 in
21 In
29 In
32 In
38 In
36 In
44 In
47 In
48 In
45 In
57ln
68ln
65 m
Maximum Flaw Rate
3 gprn
6 gprn
15 gpm
lOgpm
20 gpm
12 gpm
25gpm
15 gpm
35 gpm
33 gpm
48 gpm
50 gpm
60 gpm
60 gpm
75 gpm
100 gpm
200 gpm
Carbon Capacity
110lbs
180 Ibs
180 Ibs
250 Ibs
250 Ibs
300 Ibs
350 lb«
400 Ibs
660 Ibs
800 Ibs
1,000 Ibs
1,000 Ibs
1,500 Ibs
2,000 IbS
2,000 Ibs
3,000 to*
6,000 Ibs
Monthly
$ 24.00
45.00
70.00
66.00
110.00
200.00
145.00
210.00
350.00
360.00
350.00
465.00
445.00
545.00
755.00
875.00
1.605.00
Weekly
$ 7.00
13.00
20.00
18.00
31.00
56.00
41.00
59.00
98.00
100.00
98.00
135.00
125.00
155.00
210.00
245.00
450.00
Daily
$ 2.00
3.00
5.00
5.00
8.00
14.00
10.00
15.00
25.00
25.00
25.00
34.00
31.00
39.00
53.00
61.00
115.00
Estimated
Operating
Hourly Cost/Hr.
S .30 $
.45
.75
.75
1.00
2.00
2.00
2.00
4.00
4.00
4.00
5.00
5.00
6.00
8.00
9.00
17.00
.15
.15
.15
.15
.15
.15
.15
.15
.20
.20
.20
.25
.20
.25
.30
.30
.50
1993
§2-1
-------
REMEDIATION EQUIPMENT
VAPOR PHASE CARBON ADSORBERS
(All rates include carbon cannister, internal piping and initial carbon supply. Carbon cannisters are made of steel and internally lined
with an epoxy coating. Pumps, transfer piping, accessory instrumentation, shipping costs and electricity costs are not included. Rates are
based on one month carbon change-out. Actual carbon life is highly site specific and will vary greatly.)
Height
Manual Pow«r«d
31 in
30 in
36 in
36 in
36 in
40 in
41 in
46 in
43 in
51 in
72 In
72 in
87 In
87 in
89 In
92 in
98 in
113 in
Diameter
20 in
19 in
24 in
24 in
24 in
26 in
27 in
32 in
33 In
38 in
38ln
44 In
47 In
47 In
47 In
57 in
68 In
85 in
Maximum Flow Rote
50dm
30 dm
60dm
300dm
100dm
75dm
150dm
125dm
250dm
200dm
400dm
250dm
600 dm
600dm
600dm
1,000dm
1.500dm
2,000 dm
Carton Capacity
100 Ibs
100 Ibs
175 Ibs
175 Ibs
200 Ibs
250 Ibs
300 Ibs
400 Ibs
400 Ibs
650 Ibs
700 Ibs
1,000 lb»
1,000 lb»
1.500 Ibs
1.600 Ibs
2,600 Ibs
4.500 Ibs
6.000 Ibs
Monthly
$ 50.00
30.00
50.00
81.00
77.00
78.00
130.00
125.00
165.00
210.00
415.00
325.00
510.00
720.00
760.00
1,220.00
2.215.00
2,495.00
Weekly
$ 14.00
8.00
14.00
23.00
22.00
22.00
36.00
35.00
46.00
59.00
115.00
91.00
145.00
200.00
210.00
340.00
620.00
700.00
Daily
$ 4.00
2.00
4.00
6.00
6.00
6.00
9.00
9.00
12.00
15.00
29.00
23.00
36.00
50.00
53.00
85.00
155.00
175.00
Estimated
Operating
Hourly Cost/Hr.
$ .60 $
.30
.60
.90
.90
.90
1.00
1.00
2.00
2.00
4.00
3.00
5.00
8.00
8.00
13.00
23.00
26.00
.15
.15
.15
.15 '
.15
.15
.15
.15
.15
.15
.20
.20
.25
.30
.30
.40
.60
.70
§2-2
1993
-------
REMEDIATION EQUIPMENT
TRAY AERATORS
Number of Trays
Electric Powered
3
3
(Includes sump pump.)
4
4
(Includes sump pump)
3
3
(Includes sump pump.)
4
4
(Includes sump pump.)
6
6
(Includes sump pump.)
3
3
(Includes tump pump.)
4
4
Flow Rate
10 gpm
10gpm
10 gpm
10 gpm
15 gpm
15 gpm
15 gpm
15 gpm
15 gpm
15 gpm
20 gpm
20 gpm
20 gpm
20 gpm
Blower Capacity
150 dm
150cfm
150dm
150dm
175dm
175dm
175dm
175dm
175dm
175dm
250dm
250 win
250 dm
"250 dm
Blower Horsepower Monthly
3 $ 235.00
3 305.00
3 280.00
3 350.00
3 280.00
3 350.00
3 315.00
3 385.00
3 350.00
3 420.00
5 365.00
5 435.00
5 405.00
5 475.00
Estimated
Operating
Weekly Daily Hourly Cost/Hr.
$ 66.00 $ 17.00 $ 3.00 $ 1.00
85.00 21.00 3.00 1.10
78.00 20.00 3.00 1.10
98.00 25.00 4.00 1.20
78.00 20.00 3.00 1.10
98.00 25.00 4.00 1.20
88.00 22.00 3.00 1.15
110.00 28.00 4.00 1.25
98.00 25.00 4.00 1.20
120.00 30.00 5.00 1.30
100.00 25.00 4.00 1.20
120.00 30.00 5.00 1.35
115.00 29.00 4.00 1.25
135.00 34.00 5.00 1.40
(IndudM sump pump.)
1993
§2-3
-------
REMEDIATION EQUIPMENT
TRAY AERATORS
Estimated
Operating
Number of Trays Row Rate Blower Capacity Blower Horsepower Monthly Weekly Daily Hourly CosVHr.
Electric Powered, Continued
6
6
(Includes sump pump.)
3
3
(Includes sump pump.)
4
4
(Includes sump pump.)
3
3
(Includes sump pump.)
4
4
20 gpm
20gpm
25gpm
2Sgpm
25 Qpm
25 gpm
SOgpm
50 gpm
60 gpm
SOgpm
250dm
250 dm
300dm
300dm
300dm
300dm
600dm
600dm
600dm
MO trfn
5
5
5
5
5
5
5
5
6
5
$ 495.00 $ 140.00 $ 35.00 S 5.00 $ 1.40
565.00 160.00 40.00 6.00 1.55
450.00 125.00 31.00 5.00 1.35
540.00 150.00 38.00 6.00 1.50
525.00 145.00 36.00 5.00 1.45
615.00 170.00 43.00 6.00 1.60
625.00 175.00 44.00 7.00 1.60
720.00 200.00 50.00 8.00 1.75
720.00 200.00 50.00 8.00 1.75
815.00 230.00 58.00 9.00 1.90
(Includes sump pump.)
1993
-------
REMEDIATION EQUIPMENT
PACKED TOWER AIR STRIPPERS
(Includes blower, demister, sump pump, fiberglass reinforced plastic tower, initial supply of tower packing, and (for trailer mounted
units) tandem axle trailer. Electricity costs not included.)
T&wer Diameter
Elsctrlc Powsrtd
12"
12"
(Trailer mounted)
18'
18-
(Trailer mounted)
24"
24-
(Trailer mounted)
so-
so-
(Trailer mounted)
36'
36-
(Trailer mounted)
Toner Height
18'0"
18'0-
IB'O-
IB'O-
IB'O-
IB'O-
18'0'
18'0'
Ifl'O-
IB'O-
Water Flow Rota
10 gpm
10 gpm
25 Qpffi
25 gpm
50 gpm
50 gpm
75 gpm
75 gpm
125 gpm
125 gpm
Maximum Air Flow
350 efm
350 cfm
500dm
500 cfm
750 cfm
750 cfm
900dm
900 cfm
1,250 cfm
1,250 cfm
Estimated
Operating
Monthly Weekly Dally Hourly Cost/He
$ 145.00 $ 41.00 $ 10.00 $ 2.00 $ .65
180.00 50.00 13.00 2.00 .70
165.00 46.00 12.00 2.00 .70
205.00 57.00 14.00 2.00 .75
195.00 55.00 14.00 2.00 .75
230.00 64.00 16.00 2.00 .80
240.00 67.00 17.00 3.00 .80
280.00 78.00 20.00 3.00 .90
280.00 78.00 20.00 3.00 .90
335.00 94.00 24.00 4.00 1.00
1999
§2-5
-------
REMEDIATION EQUIPMENT
PUGMILL MIXERS
(Pugmill Mixers include mix elevator, screening unit and tandem axle trailer.)
HP
Electric Powered
140
165
190
195
245
Capacity
Manual Powered
5 GAL
5 GAL
6 GAL
5 GAL
7 GAL
7 GAL
4A AAI
10 UAL
10 GAL
10 GAL
10 GAL
Mixer Size
SO1 X 6'
50' X 6'
50' X 101
60' X 8'
60'X10'
Material
Polyethylene
Polypropylene
HOPE
fViti iniruB J— — •—
FOfypropywft*
HOPE
Polypropylene
yetnywne
Polypropylene
HOPE
Polypropylene
Mixer Type
Paddle
Paddle
Paddle
Paddle
Paddle
BINS
*»
Cylindrical Storage
Cylindrical Storage
Rectangular
Rectangular
Rectangular
Rectangular
/^.«_jj-j__i dJL . . j-.
cylindrical storage
Cylindrical Storage
Rectangular
Rectangular
Monthly Weekly
$ 4,630.00 $ 1,295.00
5,105.00 1.430.00
6,260.00 1.475.00
6,970.00 1.950.00
7,790.00 2,160.00
Monthly Mtoefcy
$ .90 $ 25
1.00 .30
1.00 .30
1.00 .30
1.00 .30
2.00 .66
4 Ml 4A
1.00 .30
2.00 .66
2.00 .55
2.00 .66
Dally
$ 325.00
360.00
370.00
490.00
545.00
Dally
$ .06
.10
.10
.10
.10
.16
4 A
.10
.16
•is.
.16
Hourly
$ 49.00
54.00
56.00
74.00
82.00
Hourly
$ .00
.00
.00
.00
.00
.00
.00
.00
.00
Estimated
Operating
CosVHr.
$ 10.30
10.90
11.10
13.35
14.45
fstfmafeo*
Operating
Cost/Hi:
S .00
.00
.00
.00
.00
.00
.00
.00
.00
§2-6
1093
-------
REMEDIATION EQUIPMENT
BINS
Capacity
Material
Type
Monthly
Estimated
Operating
Weekly Daily Hourly Cost/He
Manual Powered, Continued
15 GAL
15 GAL
15 GAL
15 GAL
25 GAL
25 GAL
25 GAL
25 GAL
35 GAL
35 GAL
50 GAL
50 GAL
55 GAL
55 GAL
55 GAL
55 GAL
55 GAL
65 GAL
66 GAL
75 GAL
76 GAL
75 GAL
Polyethylene
Polypropylene
HOPE
Polypropylene
Polyethylene
Polypropylene
HOPE
Polypropylene
HOPE
Polypropylene
HOPE
HOPE
Cron-llnfcMJ PE
Polyethylene
Polypropylene
HOPE
Polypropylene
HOPE
HOPE
Croa»4inkedPE
^ihiartii rtana
iTJiyeviyieiw
Polypropylene
Cylindrical Storage
Cylindrical Storage
Rectangular
Rectangular
Cylindrical Storage
Cylindrical Storage
Rectangular
Rectangular
Rectangular
Rectangular
Utility-Dry
Utility-Wet
Cylindrical Storage
Cylindrical Storage
CyNnoncw StoctQO
Rectangular
Rectangular
Utility-Dry
Utflity-WM
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
$ 2.00
2.00
2.00
3.00
2.00
3.00
3.00
3.00
3.00
5.00
1.00
2.00
3.00
3.00
4.00
5.00
7.00
1.00
2.00
6.00
6.00
7.00
$ .55 $
.55
.55
.85
.55
.85
.85
.65
.85
1.00
.30
.55
.85
.85
1.00
1.00
2.00
.30
.55
2.00
1.00
2.00
.15 $
.15
.15
.20
.15
.20
.20
.20
.20
.25
.10
.15
20
20
.25
25
.50
.10
.15
.50
25
.50
.00 $
.00
.00
.05
.00
.05
.05
.05
.05
.05
.00
.00
.05
.05
.05
.05
.10
.00
.00
.10
.05
.10
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.00
.05
.05
.00
.00
.05
.05
.05
1903
§2-7
-------
REMEDIATION EQUIPMENT
BINS
Capacity
Material
Tfre
Monthly
WeeUy Dally Hourty
Estimated
Operating
Cost/He
Manual Powered, Continued
75 GAL
75 GAL
80 GAL
80 GAL
100 GAL
100 GAL
100 GAL
100 GAL
100 GAL
100 GAL
100 GAL
130 GAL
130 GAL
150 GAL
150 GAL
160 GAL
160 GAL
200 GAL
9AA AaVI
200 GAL
200 GAL
250 GAL
HOPE
Polypropylene
HOPE
HOPE
Crete-linked PE
Polyethylene
Polypropylene
HOPE
noiypropywrw
HOPE
HOPE
HOPE
HOPE
Crew-linked PE
Myprepyiene
HOPE
HOPE
Crott-lnkad PE
Pofypropyton*
Rectangular
Rectangular
Utility-Dry
UtilHy-Wet
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Rectangular
Rectangular
Utility-Dry
Utfflty-Wet
Utility-Dry
Utility-Wat
Cylindrical Storage
^^- Jl 1-1 1 GtMfWMA
cyiinGnCBi storage
Cylindrical Storage
Utility-Dry
Utility-Wet
Cylindrical Storage
<%. -It— -1-1 1 ^1 1 1 1 • 1 1 •
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
$ 6.00
9.00
2.00
3.00
8.00
6.00
8.00
9.00
12.00
2.00
3.00
2.00
4.00
9.00
0 AA
B.OO
10.00
3.00
4.00
10.00
9.00
11.00
13.00
$ 2.00
3.00
.55
.85
2.00
2.00
2.00
3.00
3.00
.56
.85
.65
1.00
3.00
A AA
2.00
3.00
.85
1.00
3.00
3.00
3.00
4.00
$ .50 $
.76
.15
*>
.50
.50
.50
.76
.75
.16
20
.16
25
.76
CA
.50
.76
£6
.76
.75
.76
1.00
.10
.10
.00
.05
.10
.10
.10
.10
.10
.00
.05
.00
.05
.10
.10
.06
.05
.10
.10
.10
.15
$ .05
.05
.00
.00
.05
.05
...06,
.05
.05
.00
.00
.00
.00
.05
.05
.00
.00
.06
fir
.06
.06
.06
1993
-------
REMEDIATION EQUIPMENT
BINS
Capacity Material
Manual Powered, Continued
250 GAL Polyethylene
250 GAL Polypropylene
350 GAL Cross-linked PE
350 GAL Polypropylene
500 GAL Cross-linked PE
500 GAL Polyethylene
500 GAL Polypropylene
1.000 GAL Polyethylene
Type
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Cylindrical Storage
Monthly
$ 12.00
17.00
18.00
16.00
21.00
24.00
22.00
34.00
33.00
43.00
Weekly
$ 3.00
5.00
5.00
4.00
6.00
7.00
6.00
10.00
9.00
12.00
Dally
$ .75
1.00
1.00
1.00
2.00
2.00
2.00
3.00
2.00
3.00
Hourly
$ .10
.15
.15
.16
.30
.30
.30
.45
.30
.45
Estimated
Operating
Cost/He
$ .05
.05
.05
.05
.05
.05
.05
.10
.10
.10
OIL/WATER SEPARATORS
(Coalescing plate-typ*)
Maximum Capacity /nMOutM Ol Outlet Discharge
Manual Powered
4 gpm 1.5*
• gpm 2*
10 gpm 2*
20 gpm 2.5*
30 gpm 2.5'
40 gpm V
60 gpm 3*
2* Gravity
2' Gravity
3* Gravity
3' Gravity
3' Gravity
3* Gravity
3' Gravity
Monthly
$ 59.00
115.00
135.00
185.00
260.00
300.00
370.00
Weekly
$ 17.00
32.00
38.00
52.00
73.00
84.00
106.00
Dtfy
$ 4.00
8.00
10.00
13.00
18.00
21.00
26.00
Houity
$ .60
1.00
2.00
2.00
3.00
3.00
4.00
Estimated
Operating
Cost/He
$ .30
.35
.40
.40
.50
.55
.60
1983
§2-9
-------
REMEDIATION EQUIPMENT
OIL/WATER SEPARATORS
(Coalescing plate-type)
Maximum Capacity Inlet/Outlet OH Outlet
Electric Powered
10 gpm 2" 3'
20 gpm 2.5" 3"
30 Qpm 2.6' 3'
40 gpm 3- 3-
60 gpm 3* 3*
Maximum Flow Rate Maximum Pressure
0-25 dm 28 *H20
26-60 cfm 45 "H20
51-100 dm 52 "H20
101-150 dm 65 'H20
151-200 dm 65 'H20
201-300 dm 90 *H20
301-600 dm 105*H20
601-800 dm 90 'H20
Discharge
1/2 HP Pump
1/2 HP Pump
1/2 HP Pump
1 HP Pump
1 HP Pump
BLOWERS
fWM
3.600
3.600
3,600
3,500
3,500
3.600
3,600
3,500
Monthly
$ 285.00
335.00
405.00
455.00
526.00
Monthly
$ 16.00
18.00
20.00
26.00
38.00
62.00
73.00
95.00
Weekly
$ 80.00
94.00
115.00
126.00
145.00
Wwwfly
$ 4.00
6.00
6.00
7.00
11.00
17.00
20.00
27.00
Daily
$ 20.00
24.00
29.00
31.00
36.00
Daly
$ 1.00
1.00
2.00
2.00
3.00
4.00
5.00
7.00
Hourty
$ 3.00.
4.00
4.00
6.00
5.00
Hourly
$ .15
.16
.30
.30
.45
.60
.75
1.00
Estimated
Operating
Cost/Hr.
$ 60
.65
.75
.80
.90
Estunat&J
OpemOng
Cost/He
$ .05
.06
.05
.05
.10
.10
.15
.15
{2-10
1993
-------
REMEDIATION EQUIPMENT
GENERAL PURPOSE CONVEYORS
HP
Electric Powvred
5
6
7
10
10
15
15
20
20
20
25
30
25
25
30
Belt Length
30'
50'
30'
40'
SO1
30'
40'
SO-
SO'
40'
6ff
60'
40'
so-
so1
00n Iwdv)
18-
18-
24-
24-
24-
so-
so-
so-
36-
36-
36-
36-
42-
42'
42'
Capacity
150tph
150 tph
300 tph
300 tph
300 tph
500 tph
500 tph
500 tph
750 tph
750 tph
750 tph
760 tph
1.100 tph
1,100 tph
1.100 tph
Monthly
$ 820.00
960.00
890.00
990.00
1,065.00
1.015.00
1,065.00
1.160.00
1,100.00
1.175.00
1,200.00
1,275.00
1.440.00
1.470.00
1,515.00
Weekly
$ 230.00
270.00
250.00
275.00
300.00
285.00
300.00
325.00
310.00
330.00
335.00
355.00
405.00
410.00
425.00
DaOy
$ 58.00
68.00
63.00
69.00
75.00
71.00
75.00
81.00
78.00
83.00
84.00
89.00
100.00
105.00
105.00
Hourly
$ 9.00
10.00
9.00
10.00
11.00
11.00
11.00
12.00
12.00
12.00
13.00
13.00
15.00
16.00
16.00
cSwHtffBtf
Operating
CosVHc
$ 2.00
2.20
2.20
2.35
2.45
2.40
2.45
2.60
2.50
2.60
2.65
2.75
4.00
4.05
4.10
1993
§2-11
-------
REMEDIATION EQUIPMENT
BELT FEEDERS
Belt Length
Electric Powered
4'
6'
4'
6'
4'
6'
4'
6'
41
61
4'
6'
Decking*
Electric Powwrad
14'
ir
14'
tr
Belt Width Horsepower
18" 2
18' 2
24* 3
24- 3
30- 3
30' 3
36* 5
36* 6
42' 7
42' 7
48* 10
48' 10
VIBRATING
Screen Site Horsepower
30* 25
30* 25
35' 30
36- 30
7fe»
Bett
Ben
Ben
Bett
Bett
Bett
Ben
Bett
Bett
Bett
Bett
Bett
GRIZZLY
Monthly Woekfy Dally Hourly
$ 310.00 $ 87.00 $ 22.00 $ 3.00
335.00 94.00 24.00 4.00
330.00 92.00 23.00 3.00
350.00 98.00 25.00 4.00
335.00 94.00 24.00 4.00
380.00 105.00 26.00 4.00
360.00 100.00 25.00 4.00
405.00 115.00 29.00 4.00
405.00 115.00 29.00 4.00
435.00 120.00 30.00 6.00
460.00 130.00 33.00 5.00
470.00 130.00 33.00 5.00
FEEDERS
Number of Docks Monthly VtoeUy Daly Hourly
1
1
1
1
$ 1.785.00 $ 500.00 $ 125.00 $ 19.00
1.940.00 545.00 135.00 20.00
1,820.00 610.00 130.00 20.00
2.070.00 680.00 146.00 22.00
Operating
CosVHr.
$ .50
.50
.60
.60
.60
.65
-»*.
.65
.55
.60
.60
.60
Ettimtted
GwtWc
$ 3.46
3.66
3.60
3.76
§2-12
1993
-------
REMEDIATION EQUIPMENT
VIBRATING GRIZZLY FEEDERS
0**Unytfi
Electric Pmwrad,
20'
141
ir
20'
ir
20'
24'
24'
30'
14'
ir
14'
ir
201
14'
ir
20-
ir
20*
24'
24'
3ff
Scnon Stn
Continued
35'
42'
42'
42*
52"
52'
62'
62'
62*
30'
30*
36'
35'
35'
42*
42*
42'
62'
62*
62'
62*
62'
Horsepower
30
35
35
35
40
40
40
60
60
25
25
30
30
30
35
35
35
40
40
40
60
60
Number of Decks Monthly
1
1
1
1
1
1
1
1
1
2
2
2
2
2
2
2
2
2
2
2
2
2
$ 2.180.00
1,850.00
1.980.00
2.210.00
2.235.00
2.540.00
4.345.00
4.655.00
5.470.00
1,630.00
1.975.00
1,670.00
2.105.00
2.206.00
1,910.00
2,030.00
2,250.00
£275.00
2,565.00
4,260.00
4.555.00
6,320.00
Wsetsty
$ 610.00
520.00
555.00
620.00
625.00
710.00
1.216.00
1,305.00
1.530.00
510.00
555.00
525.00
590.00
615.00
535.00
570.00
630.00
635.00
720.00
1,195.00
1.275.00
1.490.00
DtSy
$ 155.00
130.00
140.00
165.00
165.00
160.00
305.00
325.00
385.00
130.00
140.00
130.00
150.00
165.00
135.00
145.00
160.00
160.00
180.00
300.00
320.00
375.00
Houify
$ 23.00
20.00
21.00
23.00
23.00
27.00
46.00 .
49.00
58.00
20.00
21.00
20.00
23.00
23.00
20.00
22.00
24.00
24.00
27.00
45.00
48.00
56.00
Esthn&tsd
OpsntinQ
Cost/He
$ 3.90
3.55
3.65
3.90
3.95
4.25
.«£0
6.55
7.40
3.90
4.05
3.95
4.20
4.35
4.00
4.15
4.40
4.40
4.76
6.70
7.05
7.95
1993
§2-13
-------
REMEDIATION EQUIPMENT
APRON FEEDERS
BeffUnpth
Electric Powered
10'
121
6'
V
Iff
12-
61
8'
Iff
6'
8'
Iff
S
V
Iff
8'
Belt Width
SO-
SO-
so-
so-
36-
36-
36*
36-
36-
36-
36-
42'
42-
42-
48*
48'
Horsepower
5
S
5
5
5
5
6
6
5
5
5
7
7
7
10
10
7fc»
Double Chain
Double Chain
Double Chain
Double Chain
Double Chain
Double Chain
Double Chain
Double Chain
THpte Chain
THple Chain
Thpto Chain
THple Chain
THple Chain
THple Cham
IHple Chain
THptoChaln
Monthly
S 1,665.00
1.795.00
1.390.00
1.520.00
1,715.00
1,850.00
1.440.00
1.570.00
1,845.00
1,535.00
1.685.00
2,010.00
1.675.00
1.840.00
2,150.00
1,960.00
Weekly
$ 465.00 S
505.00
390.00
425.00
480.00
520.00
405.00
440.00
516.00
430.00
470.00
565.00
470.00
616.00
600.00
650.00
DOy
115.00
125.00
98.00
105.00
120.00
130.00
100.00
110.00
130.00
110.00
120.00
140.00
120.00
130.00
150.00
140.00
Hourly
$ 17.00
19.00
15.00
16.00
18.00
20.00
15.00
17.00
20.00
17.00
18.00
21.00
16.00
20.00
23.00
21.00
E$tirntted
Opening
Cost/He
$ 1.90
2.00
1.70
1.80
1.95
2.05
1.76
1.85
10.30
8.55
9.40
11.30
9.35
10.30
12.10
11.00
12-14
1993
-------
REMEDIATION EQUIPMENT
SCALPING SCREENS
Screen Width
Eltctrlc Pmnrad
3-0-
3'6'
4'0- (Double Deck)
Operating
Screen Length HP Monthly Weekfy Dally Hourly Cost/He
B'O' 7 $ 340.00 $ 95.00 $ 24.00 $ 4.00 $ .00
8'0* 7 380.00 105.00 26.00 4.00 .00
lO'O" 15 485.00 135.00 34.00 5.00 .00
DRUM DEHEADERS
Operating
Type Cutter Diameter Drum Gauge Monthly Weekly DtOy Hourly Cost/He
Manual Powered
Hand Operated
Electric Powered
Po^ed
Air Powered
Po^ed
HP
QaeoBne Powered
6
11
16
N/A AH $ 13.00 $ 4.00 $ 1.00 $ .15 $ .00
lln 18/20 240.00 67.00 17.00 3.00 .15
1ln 18/20 265.00 74.00 19.00 3.00 .15
WALK-BEHIND ROTOT1LLERS
OpertSng
CM* THWttf) Rotor Diameter Monthly WteUy Daly Hourly CosUHt
Mechanical 18* 7* $ 62.00 $ 17.00 $ 4.00 $ .60 $ .40
HydmuSe 24* 14* 206.00 67.00 14.00 2.00 .75
HydmuBc 30* 14* 270.00 76.00 19.00 3.00 1.05
1983
§2-15
-------
REMEDIATION EQUIPMENT
SELF-PROPELLED RIDE-ON ROTOTILLERS
HP
Dnve Tin Width
Rotor Diameter Monthly
WeeMy
Dally
Hourly
Estimated
Operating
Cost/He
Gasoline Powered
12
12
12
12
19
19
19
24
24
24
24
Manual Reverting 36*
Manual Reverting 36*
Manual Reverting 42*
Manual Reverting 42*
Manual Reverting 42"
Manual Reverting 42"
Manual Reverting 50*
Hydrostatic 60"
Hydrostatic 50*
Hydrostatic 60*
Hydrostatic 60*
14"
7"
14'
17'
14'
17'
17'
17'
20-
17'
20"
$ 375.00
360.00
380.00
400.00
460.00
480.00
480.00
570.00
585.00
580.00
600.00
$ 105.00
100.00
105.00
110.00
130.00
135.00
135.00
160.00
165.00
160.00
170.00
$ 26.00
25.00
26.00
28.00
33.00
34.00
34.00
40.00
41.00
40.00
43.00
$ 4.00
4.00
4.00
4.00
6.00
5.00
6.00
6.00
6.00
6.00
6.00
$ 1.25
1.25
1.25
1.25
1.70
1.70
1.70
2.10
2.10
2.10
2.10
LOW TEMPERATURE THERMAL DESORBERS
(An units Include primary feed hopper and screens, soil conveying equipment secondary feed hoppers and mbdng equipment, controlled
weigh batchers, scalping screen, primary desorber unit, secondary vapor treatment (thermal ooddlzer), doth baghouse, treated toil
conveying equipment, and control house. Capacity Is based on 12% sod moisture content. Maximum BTU rating Is based on both desorber
and coddlzer burners. Fuel costs wfll vary with contaminant type and amount (For example, 10,000/ppm BTEX can reduce fuel requirement
by as much as four gallons propane per ton of sol.) Fuel costs assume no recycling of contaminant vapors for use as fuel.)
E$amat*t
Operating
Drum Diameter Drum Length Capacity Maximum BW Monthly Weekly Dafy Hourly Ctut/Hc
UquM Propane Oas Powirsd
(Operating cost win fluctuate due to seasonally of propane costs.)
6'6'
re*
9'6'
25'0'
36-0-
55'0'
25-50 tph
60-75 tph
75-110 tph
37,600,000
75,000,000
120,000,000
$ 26.065.00 $ 7,300.00 $ 1,825.00 $ 275.00 t 270.10
32£90.00 9,040.00 2.260.00 340.00 606.06
37,190.00 10,416.00 2,605.00 390.00 785.90
$2-16
1993
-------
REMEDIATION EQUIPMENT
LOW TEMPERATURE THERMAL DESORBERS
(All units Include primary feed hopper and screens, soil conveying equipment, secondary feed hoppers and mixing equipment, controlled
weigh batchers, scalping screen, primary desorber unit, secondary vapor treatment (thermal oxidizer), cloth baghouse, treated soil
conveying equipment, and control house. Capacity Is based on 12% soil moisture content. Maximum BTU rating is based on both desorber
and oxldizer burners. Fuel costs will vary with contaminant type and amount. (For example, 10,000/ppm BTEX can reduce fuel requirement
by as much as four gallons propane per ton of soil.) Fuel costs assume no recycling of contaminant vapors for use as fuel.)
Estimated
Operating
Capacity Maximum BTU Monthly Weekly Dally Hourly Cost/He
Down Diameter Drum Length
DtoMlPmwred
5'6- 25'0-
re- 35-0-
re1
Natural Gat Povwrad
8'e-
re- 35-0-
re-
25-50 tph
50-76 tph
75-110 tph
25-50 tph
60-76 tph
75-110 tph
37,500.000 $ 26.065.00 $ 7.300.00 $ 1,825.00 $ 275.00 $ 321.00
75,000,000 32,290.00 9.040.00 2.260.00 340.00 606.20
120.000.000 37.190.00 10.415.00 2.605.00 390.00 948.25
37,600,000 26.065.00 7,300.00 1.825.00 275.00 310.60
75,000,000 32,290.00 9,040.00 2,260.00 340.00 589.00
120,000,000 37,190.00 10,415.00 2.605.00 390.00 921.45
SOIL VAPOR EXTRACTION SYSTEMS
(Includes moisture separator, automatic shut-off device, air fitter, and Inlet manifold. Skid mounted. Flow Instrumentation and
electricity costs not Included.)
Estimated
Operating
Pump Capacity Horsepower Intake Diameter Maximum Vacuum Monthly WteHy Daly Hourly CoaVHc
Electric
76 dm 1
(With 20 gallon moMura Mparatoc)
76dm 1
(With 40 gallon moMura •aparatoc)
160dm 2
(With 20 gallon moteture separatee)
160dm 2
(WUh 40 gallon moisture Mparatoc)
48-H20 $ 115.00 $ 32.00 $ 8.00 $ 1.00 $ .30
48*H20 120.00 34.00 9.00 1.00 .30
60-H20 125.00 36.00 9.00 1.00 .30
60'h20 130.00 36.00 9.00 1.00 .30
1083
§2-17
-------
REMEDIATION EQUIPMENT
SOIL VAPOR EXTRACTION SYSTEMS
(Includes moisture separator, automatic shut-off device, air filter, and inlet manifold. Skid mounted. Flow instrumentation and
electricity costs not Included.)
Vacuum Pump Capacity Horsepower Intake Diameter
Electric Powered (Continued)
250 dm 6 2'
(With 20 gallon moisture separator.)
250 dm 5 2*
(With 40 gallon moisture separator.)
400dm 10 2*
(With 20 gallon moisture separatee)
400dm 10 2'
(With 40 gallon moisture separator.)
Airflow Number of Baga Horsepom
Electric Powered
20.000 CFM 280 80
25.000 CFM 280 100
35.000 CFM 336 170
50.000 CFM 560 210
55,000 CFM 704 230
65.000 CFM 704 270
75.000 CFM 800 280
Maximum Vacuum
90-H20
90-H20
90'H20
90*H20
BAGHOUSES
tr Number ol Axle*
2
2
2
3
3
3
3
Monthly Weekly Daily
$ 185.00 $ 52.00 $ 13.00
190.00 53.00 13.00
310.00 87.00 22.00
315.00 88.00 22.00
Monthly WeeMy Daly
$ 7.130.00 $ 1.995.00 $ 500.00
7,310.00 2.045.00 510.00
8.625.00 2,470.00 620.00
11.355.00 3.180.00 795.00
13,470.00 3.770.00 945.00
13.300.00 3,725.00 930.00
14,510.00 4.065.00 1,015.00
Estimated
Operetfao.
Hourly Cost/Hr.
$ 2.00 $ .35
2.00 .35
3.00 .45
3.00 .45
CMrTUfiVu
Operating
Hourly CotVHt
$ 75.00 $ 12.45
77.00 1Z60
93.00 16.60
120.00 18.95
140.00 24.80
140.00 27.45
150.00 28.65
§2-18
1993
-------
REMEDIATION EQUIPMENT
WET SCRUBBERS
Air Flow
20.000 CFM
30,000 CFM
40.000 CFM
65.000 CFM
70,000 CFM
Horsepower
120
180
230
350
450
Monthly
$ 2,410.00
3,100.00
6,390.00
6,825.00
7.405.00
Weekly
$ 675.00
870.00
1.790.00
1.910.00
2,075.00
Dfily
% 170.00
220.00
450.00
480.00
520.00
Hourly
$ 26.00
33.00
68.00
72.00
78.00
C£JVTUU9Cr
Opontiny
Cost/He
$ 5.20
5.85
12.90
13.30
13.80
LOCATORS
TTanarnfller Optnting
Typ» Rooatvfr Output Output ftmer Source Monthly Weekfy DtSfy Hourly Cost/He
Electric towered
Magnetic
Magnetic and Cable
40 HZ M/A C-Cell Batteriee $ 62.00 $ 17.00 $ 4.00 $ .60 $ .15
40 HZ 82 KHZ OCeO Batteriee 175.00 49.00 12.00 2.00 .25
SKIMMERS
(Electric models Include product bladder pump and controller.)
Monthly
Optathg
DOy Hourly CosVHc
Manual Poinered
3h
tin
1993
DovmhoJe
Downhoto
Downhole
$ 75.00 $ 21.00 $ 6.00 $ .75 $ .06
91.00 25.00 8.00 .90 .05
245.00 69.00 17.00 3.00 .40
§2-19
-------
REMEDIATION EQUIPMENT
DOWNHOLE FILTER-SEPARATORS
(Includes product pump and controller.)
Pump Diameter
Electric Powered
4 in
4 in
6tn
6 In
Operating
Recovery Rate Control Panel Monthly Watty Dairy Hourly CostfHr.
.300pm NEMA3 $ 310.00 S 87.00 $ 22.00 $ 3.00 $ .55
.30gpm NEMA7 365.00 100.00 25.00 4.00 .60
.60gpm NEMA3 355.00 99.00 25.00 4.00 .60
.60gpm NEMA7 405.00 115.00 29.00 4.00 .65
SURFACE FILTER-SEPARATORS
Estimated
Operating
Recovery*** Buoy Diameter Monthly Mfevty Daly Hourly Co*t/Ht
Electric PtMMmd
Sgpm
18 In
$ 350.00 $ 98.00 $ 25.00 $ 4.00 $ .50
BLADDER PUMPS
Mudmum Flow Re* PumpDdmtttf
Ungtfi
Estifnettd
OptoOng
Dtp* Ctptdty Monthly WMdy Mfy Houfy OoH/Hc
Air Powered
2gpm
(StaNeMcteeO
2gpm
(Stainless steel)
2gpm
(Stainless eteel)
2gpm
(Teflon)
1ln
1ln
1h
1ln
36k)
36k)
36 In
36ln
100'
2S'
SO'
100*
$ 115.00 $ 32.00 $ 8.00 $ 1.00 1 .40
106.00 29.00 7.00 1.00 .35
105.00 29.00 7.00 1.00 .40
120.00 34.00 9.00 1.00
.40
52-20
1993
-------
REMEDIATION EQUIPMENT
BLADDER PUMPS
Maximum Flow Rate Pump Diameter
Air Powered, Continued
2 gpm 1 in
(Teflon)
2gpm 1 in
(Tenon)
4gpm iin
(Stainless steel)
*OP"» 1ln
(Stainless steel)
4gpm 1 1n
(Stainless steel)
4gpm iin
(Teflon)
4gpm 1 1n
(TMon)
4gpm 1 1n
Hefton)
L«n0fn
36 In
36 In
98 In
96 In
08 hi
98 In
98 In
98 In
Depth Capacity Monthly
25' $ 110.00
50' 110.00
100' 125.00
25' 110.00
50' 115.00
100' 130.00
25' 115.00
60' 120.00
Estimated
Operating
WseHy Daffy Hourly Cost/He
$ 31.00 $ 8.00 $ 1.00 $ .40
31.00 8.00 1.00 .40
35.00 9.00 1.00 .40
31.00 6.00 1.00 .40
32.00 8.00 1.00 .40
36.00 9.00 1.00 .45
32.00 8.00 1.00 .40
34.00 9.00 1.00 .40
CENTRIFUGAL PUMPS
HP Sto
GttoQiw Pomrad
3 2"
3 2'
6 2*
6 2'
7 2'
7 2'
Capacity
115 gpm
116-gpm
135 gpm
135 gpm
165 gpm
165 gpm
Mounting Monthly
SMd $ 75.00
IMIer 69.00
SUd 83.00
trailer 100.00
SUd 120.00
trailer 150.00
Estimated
Operating
WeeUy Daly Hourly Coal/He
$ 21.00 $ 5.00 $ .75 $ .35
25.00 6.00 .90 .40
23.00 6.00 .90 .55
28.00 7.00 1.00 .55
34.00 9.00 1.00 .80
42.00 11.00 2.00 .80
1999
§2-21
-------
REMEDIATION EQUIPMENT
CENTRIFUGAL PUMPS
HP Size
Diesel Powered, Continued
3 1.6-
3 1.5'
7 3'
7 3-
10 3-
6 2'
10 3'
Maximum Pressure Dn\»
60 pel Direct Current
100 pti Direct Currant
100 pel Highspeed
100 ptl Low Speed
100 pel Synchnnoue
60 pel Variable Speed
100 pal Variable Speed
Capacity
85 gpm
85 gpm
250 gpm
250 gpm
300 gpm
135 gpm
300 gpm
CHEMICAL
Murfmum Flow fitfe
60-500 MLMN
60-600 MLMN
60-600 MLMN
0-60 MLMN
0-60 MLMN
600-1000 MLMN
50-600 MLMN
Mounting
Skid
Trailer
Skid
Trailer
Trailer
Trader
Trailer
METERING
WettodPut*
Ceramic
Ceramic
Ceramic
Cemmte
Ceramic
Ceramic
Ceramic
Monthly
$ 72.00
87.00
155.00
170.00
390.00
190.00
360.00
PUMPS
Monthly
$ 38.00
49.00
44.00
62.00
63.00
64.00
70.00
Weekly
$ 20.00
24.00
43.00
48.00
110.00
63.00
100.00
WMMy
$ 11.00
14.00
12.00
16.00
18.00
16.00
20.00
DaBy
$ 5.00
6.00
11.00
12.00
28.00
13.00
25.00
Da*
$ 3.00
4.00
3.00
4.00
6.00
6.00
6.00
Estimated
Operating
Hourly Coat/He
$ .75 $ .35
.90 .40
2.00 .85
2.00 .85
4.00 1.25
2.00 .60
• '" • ^
4.00 .90
Hourly Cost/He
$ .46 $ .10
.60 .10
.46 .10
.60 .10
.76 .16
.76 .16
.75 .15
100 pel
Pnoumcttc
0-200
Ceramic
66.00
19.00
6.00
.76
.16
§2-22
1993
-------
REMEDIATION EQUIPMENT
DIAPHRAGM PUMPS
DfectopoSto
Air Powered
3/4'
3/4'
f
1*
1-1/4'
MM'
1/2'
1/2'
r
2'
3'
3'
Motor Mit0/ii/
Aluminum
Aluminum
Aluminum
Alumlnim
Aluminum
Aluminum
Aluminum
Aluminum
Aluminum
Aluminum
Aluminum
Aluminum
Ctptcdty
30 gpm
30 gpm
'40 gpm
40 gpm
60 gpm
50 gpm
16 gpm
16 gpm
160 gpm
150 gpm
220 gpm
220 gpm
Ball/Dlaphmgm Monthly
Noopron6 $ 27.00
Teflon 38.00
Neopiene 29.00
Teflon 47.00
Neoprene 35.00
Teflon 53.00
Neoprene 17.00
Teflon 21.00
NMpmw 89.00
Teflon 67.00
Neoprene 80.00
Teflon 110.00
WeeUfy
$ 8.00
11.00
8.00
13.00
10.00
15.00
5.00
6.00
19.00
24.00
22.00
31.00
Daly
$ 2.00
3.00
2.00
3.00
3.00
4.00
1.00
2.00
6.00
6.00
8.00
6.00
Houity
$ .30
.45
.30
.45
.45
.60
.15
.30
.76
.90
.90
1.00
Cost/He
$ .15
.15
.15
.15
.15
.15
.10
.10
JO
.20
.20
.25
1993
§2-23
-------
REMEDIATION EQUIPMENT
SUBMERSIBLE PUMPS
Pump Size
ElMtric Povmrad
2'
4-
4-
4"
4'
4-
4'
4'
4-
4'
4'
4-
4*
Horsepower Maximum Capacity
2.00 9 gpm
.50 7 gpm
1.00 7 gpm
1.60 7 gpm
.60 14 gpm
1.00 14 gpm
1.60 14 gpm
.50 20 gpm
1.00 20 gpm
1.60 20 gpm
.50 32gpm
1.00 32 gpm
1.50 32 gpm
Discharge Size
1/2-
r
1-
1-
1-1/4-
1-1/4-
1-1/4-
1-1/4-
1-1/4-
1-1/4-
1-1/2*
1-i/r
M/r
Monthly
$ 155.00
99.00
115.00
145.00
100.00
120.00
140.00
99.00
110.00
130.00
99.00
110.00
130.00
WeoUy Dafy Hourly
$ 43.00 $ 11.00 $ 2.00
28.00 7.00 1.00
32.00 8.00 1.00
41.00 10.00 2.00
28.00 7.00 1.00
34.00 9.00 1.00
39.00 10.00 2.00
28.00 7.00 1.00
31.00 8.00 1.00
36.00 9.00 1.00
28.00 7.00 1.00
31.00 8.00 1.00
38.00 9.00 1.00
EtOmated
Cost/He
$ .15
.15
.15
.15
.16
.15
.15
•1.5
.16
.16
.16
.15
.16
THERMAL OXIDIZERS
T&npontum Ring* (F)
Ductile Powtrtd
1400-1500
(SUd mounted)
1400-1500
fliitor mounted)
Maximum Air now
1,000 dm
1,000dm
Retention Ttm»
1 Second
ISaoond
Monthly
$ 1,706.00
1,820.00
Mfcety Daly Hourly
$ 476.00 $ 120.00 $ 18.00
510.00 130.00 20.00
Cott/Hc
$ 2.70
2.85
»2-24
1993
-------
REMEDIATION EQUIPMENT
THERMAL OXIDIZERS
Temperature Range (F)
Maximum Air Flow
Retention Time
Monthly WeoHy
Estimated
Operating
DaHy Hourly Cost/He
Electric Powered (Continued)
1400-1500
(Skid mounted)
1400-1500
(Traitor mounted)
1400-1500
(Sldd mounted)
1400-1500
(Trailer mounted)
250dm 1 Second $ 1,185.00 S 330.00 $ 83.00 $ MOO $ 2.15
250dm 1 Second 1.270.00 355.00 89.00 13.00 2.25
600dm 1 Second 1.350.00 380.00 95.00 14.00 2.35
500dm 1 Second 1.445.00 405.00 100.00 15.00 2.45
CATALYTIC OXIDIZERS
(Operating costs do not Include catalyst replacement.)
Temperature Range (F) Maximum Mr Flow
Catafytt
Operating
Met Diameter Monthly WseUy Daly Hourly Cost/He
400-000 250dm Platinum Coated
(SUd mounted)
400-000 250dm Platinum Coated
(Tnier mounted)
400400 600 dm Platinum Coated
(SUd mounted)
400400 600dm Platinum Coated
(Iraler mounted)
4* $ 1.465.00 $ 410.00 I 105.00 $ 16.00 $
4* 1,645.00 435.00 110.00 17.00
4* 1,656.00 620.00 130.00 20.00
4* 1,945.00 645.00 135.00 20.00
6.65
7.00
8.25
6.60
1M3
§2-25
-------
REMEDIATION EQUIPMENT
FIXED FILM BIOREACTORS
(External piping, pump, blower, bacteria and electricity costs are not included.)
Diarrwtar
Electric Powered
48'
60'
72'
108*
132'
HP
65
80
95
OMMU fnowvfvo
74
05
100
276
Height Maximum Air Flow Maximum Water Flow Monthly WeoUy Dairy Hourly
T 16 dm 7 gpm
8' 20 dm 12 gpm
9' 30 dm 30 gpm
9' 65 dm 65 gpm
10' 95 dm 95 gpm
ROTARY AUGER DRILLS FOR
Maximum To/put Maximum Pulldown
3,500 FMbe 10.000 be
6.250 FMbe 25.000 be
10,000 R-lbt 30.000 be
3,600 FMbe 10.000 be
6.250 FHbe 25.000 be
10.000 Ft-b* 30,000 be
20.000 Ft-be 35.000 be
$ 450.00 $ 125.00 $ 31.00 $ 5.00
665.00 165.00 46.00 7.00
870.00 245.00 61.00 9.00
1,025.00 285.00 71.00 11.00
1.145.00 320.00 80.00 12.00
TRUCK MOUNTING
Monthly VtoeHy Daly Hourly
$ 2,435.00 t 660.00 $ 170.00 $ 26.00
4840.00 795.00 200.00 30.00
4.700.00 1.315.00 330.00 50.00
2,660.00 745.00 166.00 28.00
2,810.00 785.00 196.00 29.00
4.925.00 1,380.00 345.00 52.00
8.440.00 2.365.00 590.00 89.00
Esttmattd
Operating
CoaVHf
$ .70
.60
.90
1.00
1.05
cstifttatto
Ofxsnting
Cott/Hc
$ 9.05
10.65
13.30
7.96
6.90
10.85
20.55
(7-26
1993
-------
REMEDIATION EQUIPMENT
TRAILER MOUNTED ROTARY AUGER DRILLS
HP Maximum Torque
Gasoline Powered
30 l.500FMte
Diesel Powered
60 LSOOFMbe
Maximum Pulldown Tteflw
4.500 Ibs Tandem Axle
4,500 Ibe Tandem Axle
Monthly
$ 980.00
1.070.00
Estimated
Operating
WeeHy Duty Hourly Cost/He
$ 275.00 $ 69.00 $ 10.00 $ 4.20
300.00 75.00 11.00 4.10
SMALL GENERATORS
HP
Gasoline Powered
1
1
2
2
3
3
3
3
4
4
6
8
7
7
Output
900W
1.000 W
1.400 W
1.600W
1.600W
2.000 W
2.100 W
2.400 W
2.500 W
3.000 W
3.600 W
4.000 W
6.000 W
6.600 W
Monthly
$ 60.00
62.00
66.00
68.00
60.00
62.00
67.00
82.00
64.00
92.00
100.00
116.00
125.00
140.00
Opening
WHeUy Oily Houity Cost/Hi
$ 14.00 $ 4.00 $ .60 $ .30
15.00 4.00 .60 .35
16.00 4.00 .60 .40
16.00 4.00 .60 .50
17.00 4.00 .60 .55
17.00 4.00 .60 .60
19.00 6.00 .76 .60
23.00 6.00 .90 .65
24.00 6.00 .90 .65
26.00 7.00 1.00 .70
28.00 7.00 1.00 .80
32.00 6.00 1.00 .65
36.00 9.00 1.00 1.00
39.00 10.00 2.00 1.15
1003
§2-27
-------
REMEDIATION EQUIPMENT
SMALL GENERATORS
HP
OMOIIIW Prnwrad (ConttniMd)
8
10
13
14
17
17
21
28
DteMl Amwmd
5
6
6
8
60
Output
6,000 W
7,500 W
9,000 W
10,000 W
12,000 W
12.500 W
15,000 W
20,000 W
2,500 W
3,000 W
4.600 W
6.000 W
17,600 W
Monthly
$ 145.00
175.00
205.00
255.00
290.00
310.00
380.00
565.00
115.00
216.00
260.00
370.00
605.00
MM*
$ 41.00
49.00
57.00
71.00
81.00
87.00
105.00
160.00
32.00
60.00
73.00
106.00
170.00
Dalfy
$ 10.00
12.00
14.00
18.00
20.00
22.00
26.00
40.00
8.00
16.00
18.00
26.00
43.00
Hourly
$ 2.00
2.00
2.00
3.00
3.00
3.00
4.00
6.00
1.00
2.00
3.00
4.00
6.00
Esti/nttod
Operating
CosVHr.
$ 1.25
1.50
1.80
2.06
2.40
2.45
2.90
4.00
.60
.60
.70
.90
4.15
LARGE GENERATORS
HP
QuellM Powmd
30
36
42
60
67
Output
20 KW
25 KW
30 KW
36 KW
40 KW
Month*
$ 430.00
446.00
496.00
635.00
555.00
MM*
$ 120.00
126.00
140.00
160.00
165.00
My
$ 30.00
31.00
35.00
38.00
39.00
Hourly
$ 6.00
6.00
6.00
6.00
6.00
Ettlmtttd
OotUHt
$ 4.30
5.00
5.70
6.66
7.40
82-26
1993
-------
REMEDIATION EQUIPMENT
LARGE GENERATORS
HP
Qasollrw Pmrarad (Continued)
64
70
78
65
92
99
106
121
142
164
176
26
43
67
64
66
107
126
143
160
176
214
280
Output
45 KW
50 KW
55 KW
60 KW
66 KW
70 KW
75 KW
85 KW
100 KW
116 KW
125 KW
20 KW
30 KW
40 KW
45 KW
60 KW
76 KW
90 KW
100 KW
110 KW
126 KW
160 KW
176 KW
Monthly
$ 605.00
630.00
675.00
705.00
760.00
815.00
865.00
895.00
955.00
1,435.00
1,430.00
560.00
710.00
750.00
860.00
920.00
1,075.00
1,120.00
1.140.00
1.250.00
1.386.00
1,420.00
1.456.00
Waekfy
$ 170.00
175.00
190.00
195.00
215.00
230.00
240.00
250.00
265.00
400.00
400.00
155.00
200.00
210.00
240.00
260.00
300.00
315.00
320.00
350.00
390.00
400.00
405.00
Dtfy
$ 43.00
44.00
48.00
49.00
54.00
58.00
60.00
63.00
66.00
100.00
100.00
39.00
50.00
53.00
60.00
65.00
75.00
79.00
80.00
86.00
98.00
100.00
100.00
Houity
$ 6.00
7.00
7.00
7.00
8.00
9.00
9.00
9.00
10.00
16.00
15.00
6.00
8.00
8.00
9.00
10.00
11.00
12.00
12.00
13.00
16.00
15.00
15.00
Estimated
Opening
Cost/He
$ 8.15
8.85
10.00
10.75
11.55
12.45
13.20
V..86
17.25
20.60
22.05
2.65
3.65
4.35
4.80
6.20
7.60
6.65
9.60
10.90
11.95
13.95
15.90
1993
(2-29
-------
REMEDIATION EQUIPMENT
LARGE GENERATORS
HP
OI«Ml Powtrwl (Continued)
285
320
357
385
428
620
670
640
713
855
900
930
1.050
1.125
1.176
1,260
1.428
Output
200 KW
225 KW
250 KW
270 KW
300 KW
365 KW
400 KW
460 KW
600 KW
600 KW
825 KW
660 KW
750 KW
600 KW
640 KW
900 KW
1,000 KW
Monthly
$ 1.510.00
1.780.00
1.910.00
1.976.00
2,060.00
2,476.00
2.760.00
3.175.00
3,650.00
4,475.00
4.505.00
4.645.00
4.836.00
4.925.00
5.216.00
6.360.00
6,065.00
WaeHy
$ 425.00 $
500.00
535.00
555.00
675.00
695.00
776.00
890.00
1.020.00
1.255.00
1.260.00
1,300.00
1,355.00
1.380.00
1.460.00
1.600.00
1.700.00
Dally
105.00
125.00
135.00
140.00
145.00
175.00
195.00
225.00
256.00
316.00
315.00
325.00
340.00
346.00
365.00
375.00
425.00
Hourly
$ 16.00
19.00
20.00
21.00
22.00
26.00
29.00
34.00
36.00
47.00
47.00
49.00
61.00
62.00
66.00
66.00
64.00
EstifnMt9d
OpeaOhg
CortHt
$ 17.85
20.65
22.75
24.30
26.70
32.00
34.90
41.70
46.00
54.35
57.80
69.66
66.16
70.30
73.30
77.46
67.46
12-30
1993
-------
COST GUIDE
FOR
REMEDIATION EQUIPMENT
AT
UST SITES
§3, APPENDICES
JULY 1993
-------
CONTENTS
Section 3: Appendices
Title Page
Appendix A: Rate Adjustment And Rate Element Tables 3-1
Appendix B: Unit Price Information For Materials Purchased For One Time Use 3-4
Appendix C: Chemical Conversion Factors 3-9
Appendix D: Equivalencies
Dl: Weight And Measure Equivalencies 3-10
. D2: Energy Equivalencies 3-12
D3: Mechanical-Electrical Equivalencies 3-12
Appendix E: Power Required For Pumping 3-13
Appendix F: Variables For Pumping Applications 3-15
1983
-------
APPENDIX A
RATE ADJUSTMENT TABLES
EQUIPMENT TYPES
ADSORBERS
AERATORS
MIXERS
BINS/TANKS
BLOWERS & FANS
CONVEYORS
DRUM DEHEADERS
ENHANCED VOLITALIZATION
DUST COLLECTION
LOCATORS, PIPE/VALVE/CABLE
OIL SKIMMERS
PUMP
OXIDIZERS
BIOREACTORS
WELL DRILLING EQUIPMENT
GENERATORS
1984
.852
.901
.925
.907
.920
.931
.944
.927
.913
.873
i .880
.852
.933
.888
.912
.910
Table 1
(1984-1993)
1985 1986 1987
.869
.913
.933
.918
.929
.937
.950
.935
.921
.888
.894
.857
.941
.901
.913
.915
.884
.923
.941
.927
.938
.943
.956
.943
.921
.901
.906
.859
.948
.912
.913
.923
.896
.931
.947
.935
.944
.948
.960
.948
.924
.911
.916
.865
.953
.921
.915
.924
1988
.908
.939
.953
.942
.950
.960
.965
.954
.928
.921
.925
.679
.958
.930
.915
.935
1989
.928
.952
.963
.955
.961
.960
.972
.964
.940
.938
.941
.907
.967
.945
.927
.954
1990
.958
.972
.979
.974
.977
.973
.984
.979
.956
.964
.966
.940
.981
.968
.947
.978
1991
.982
.988
.991
.989
.990
.980
.993
.991
.969
.984
.985
.955
.992
.986
.971
.992
1992
.998
.999
.999
.999
.999
.992
.999
.999
.985
.998
.999
.979
.999
.999
.991
.997
1993
1.000
1.000
1.000
1.000
1.000
1.000
1.000
t.ooo
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1908
S3-1
-------
APPENDIX A
RATE ADJUSTMENT TABLES
EQUIPMENT TYPES
ADSORBERS
AERATORS
MIXERS
BINS/TANKS
BLOWERS & FANS
CONVEYORS
DRUMS DEHEADERS
ENHANCED VOLITALIZATION
DUST COLLECTION
LOCATORS, PIPE/VALVE/CABLE
OIL SKIMMERS
PUMP
OXIDIZERS
BIOREACTORS
WELL DRILLING EQUIPMENT
GENERATORS
1974
.428
.618
.709
.641
.691
.693
.781
.716
.795
.509
.537
.675
.742
.567
.788
.736
Table 2
(1974-1983)
1975 1976 1977
.473
.648
.732
.670
.715
.724
.799
.738
.802
.547
.573
.684
.762
.601
.798
.764
.530
.686
.761
.705
.746
.742
.820
.767
.814
.596
.619
.696
.788
.644
.803
.779
.554
.703
.773
.721
.759
.757
.830
.779
.829
.617
.639
.711
.799
.663
.832
.795
1978
.583
.722
.788
.738
.775
.773
.841
.793
.843
.642
.662
.730
.812
.684
.843
.803
1979
.619
.746
.806
.761
.794
.789
.855
.611
.860
.673
.692
.751
.828
.712
.847
.818
1980
.665
.777
.830
.790
.819
.835
.872
.834
.883
.713
.729
.806
.849
.747
.876
.833
1981
.732
.821
.864
.832
.855
.860
.898
.867
.902
.770
.783
.839
.879
.797
.897
.863
1982
.793
.862
.895
.870
.888
.901
.921
.897
.908
.822
.832
.848
.906
.843
.910
.886
1983
.833
.889
.915
.895
.910
.921
.936
.917*
.908
.857
.865
.843
.925
.874
.912
.892
1003
-------
APPENDIX A
RATE ELEMENT TABLE
Table 3
The Rate Element Table is designed to allow for greater accuracy when adjusting Cost Guide rates and
identifying specific cost allowances contained in the rates. The basic Cost Guide rate contains allowances for
depreciation, major overhaul repairs, cost of facilities capital (Cfc), and indirect costs. These tables show the
percentage of the total Cost Guide rate that each cost allowance comprises. See section 1, "INTRODUCTION,"
for a complete explanation of the Rate Element Table and sample applications.
Equipment types
ADSORBERS
AERATORS
MIXERS
BINS/TANKS
BLOWERS & FANS
CONVEYORS
DRUMS DEHEADERS
ENHANCED VOLITALIZATION
DUST COLLECTION
LOCATORS. PIPE/VALVE/CABLE
OIL SKIMMERS
PUMP
OXIDIZERS
BIOREACTDRS
WELL DRILLING EQUIPMENT
GENERATORS
Major
Depreciation Overhaul
.89
.60
.46
.50
.51
.43
.41
.26
.37
.75
.71
.55
.40
.68
.39
.37
.00
.09
.25
.05
.22
.36
.32
.13
.34
.04
.05
.21
.14
.12
.26
.28
Cfc
.06
.10
.10
.16
.10
.08
.11
.18
.10
.10
.10
.10
.'!4
.08
.12
.14
Indirect
Costs
.05
.21
.19
.29
*•»
.17
.13
.16
.43
.19
.11
.14
.14
.32
.12
.23
.21
1089
-------
APPENDIX B
Unit Price Information For Materials Purchased For One Time Use
Bailers
TEFLON
Standard Top, 1.875" O.D $40.50
Point Sampling Top, 1.875" O.D $67.50
12" Extension Tube, 350 cc, 1.75" O.D $42.40
24" Extension Tube, 700 cc, 1.75".OJ) $83.80
36" Extension Tube, 1.050 cc, 1.75" O.D $98.20
Extension Coupling $18.75
Standard Bottom, 1.875" O.D $37.40
Bottom Emptying Bottom, 1.875" OX) $56.00
Control Flow Bottom, 1.875" O.D $68.90
.75" O.D. x V, 60 cc, complete bailer $129.30
.75" O.D. x 3', 180 cc, complete bailer $164.60
1" O.D. x 1', 80 cc, complete bailer $180.30
1" O.D. x3', 240 cc, complete bailer. $211.00
Economy bailer, 1.75" O.D. x I1, complete $53.50
Economy bailer, 1,75" O.D. x 3', complete $89.90
(Economy bailers include a lifting cap and standard bottom.)
Teflon suspension cord $1.10/foot
PVC
Standard Bailer, 1.66" O.D. x 12", 300 cc $18.20
Standard Bailer, 1.66" OX), x 24", 600 cc $19.25
Standard Bailer, 1.66" OX), x 36", 900 cc $22.00
Standard bailer, 3.5" OJ). x 12", 1,450 cc $42.00
Standard bailer, 3.5" OX), x 24", 2,900 cc $45.20
Standard bailer, 3.5" OX), x 36", 4,350 cc $48.00
(Standard bailers include PVC lifting cap and standard bottom.)
PVC valve bottom emptying device, 1.66" OD $28.50
PVC valve bottom emptying device, 3.5* OX) $90.40
Teflon valve bottom emptying device, 3.5" O.D $138.00
1003
-------
APPENDIX B
Unit Price Information For Materials Purchased For One Time Use
Well Supplies
Cement
Ready Mix Concrete, 90# bag $3.25
Portland Cement, 90# bag $7.00
Grout
Bentonite Grout, 50# bag $22.50
Bentonite Chips, 50# bag $7.50
Bentonite, granular, 50# bag $6.25
Bentonite Donuts, package of four $115.00
Bentonite Tablets, 50# bag $31.00
Grouting Tremie Pipes
5'PVC, 1.3" ID. x 1.05" OJ> $7.25
10'PVC, 1.3" I.D. x 1.05" OD $10.95
Manholes
CAST IRON
6" OJ>. x7" deep $49.25
8" OJD. x 8" deep $55.35
12" OJX x 12" deep $77.35
Sand
Monterey Sand, 4 x 12 Mesh, 100* bag $6.12
Monterey Sand, 8 x 20 Mesh, 100# bag $4.75
Monterey Sand, 20 x 40 Mesh, 100# bag $4.35
Silica Sand, All Mesh, 100# bag $3.55
Well Caps
PLASTIC
2", Locking $15.45
4", Locking $18.15
6", Locking $35.75
193 §3-5
-------
APPENDIX B
Unit Price Information For Materials Purchased For One Time Use
Well Caps
CAST ALUMINUM
2",W/Padlock $16.75
4",W/Padlock $18.75
6",W/Padlock $25.50
8", W/ Padlock $34.50
Well Casing
PVC SCHEDULE 40
1" LDx 10' $10.90
1.5" I.D. x W $13.50
2" I.D. x 10' $17.00
4" ID. x 10' $42.10
5" LD. x 10' $58.50
6" LD. x 10' $92.15
PVC SCHEDULE 80
.75" LD. x Iff $11.00
1" LD. x 10* $11.25
2" LD. x Iff $23.55
4" LD. x Iff $58.80
PVC SCHEDULE 80
5" LD. x 10- $95.80
6" LD. x Iff $129.20
STAINLESS STEEL TYPE 304
2" LD. x W $108.50
4" LD. x Iff $260.00
5" LD. x Iff $415.00
6" LD. x Iff $610.00
8" LD. x 10- $850.00
STAINLESS STEEL TYPE 316
2" LD. x Iff $165.00
4" ID. x Iff $310.00
(34 1993
-------
APPENDIX B
Unit Price Information For Materials Purchased For One Time Use
Well Casing
TEFLON SCHEDULE 40
2" I.D. x 10' $301.00
4" I.D. x 10' $925.00
TEFLON SCHEDULE 80
2" I.D. x 10' $395.00
4" LD. x 10' $1,145.00
Well Covers
4" x 51, W/Padlock $56.50
6" x 5', W/ Padlock $76.40
8" x 5', W/Padlock. $114.15
10" x 5', W/Padlock $152.25
12" x 5', W/Padlock $162.75
Well Screen
PVC SCHEDULE 40
r ID. x 101 $19.70
1.5" LD. x Iff $25.25
2" LD. x Iff $27.90
4" LD. x Iff $64.05
5" LD. x Iff $85.00
6" LD. x Iff $108.10
PVC SCHEDULE 80
.75" LD. x Iff $20.15
1" LD. x Iff $21.50
2" LD. x Iff $40.85
4" LD. x Iff $97.25
5" LD. x Iff $120.10
6" LD. x Iff $152.40
STAINLESS STEEL TYPE 304
2" LD. x Iff $302.50
4" LD. x Iff $450.00
5" LD. x Iff $580.00
6" LD. x Iff $845.00
8" LD. x Iff $1.545.00
1988 §3-7
-------
APPENDIX B
Unit Price Information For Materials Purchased For One Time Use
Well Screen
STAINLESS STEEL TYPE 316
2" I.D. x 10' $425.00
4" ID. x 10' $590.00
TEFLON SCHEDULE 40
2" ID. x Iff $390.00
4" I.D. x 10' $1,154.50
TEFLON SCHEDULE 80
2" LD. x Iff $517.00
4" LD. x 10' $1,386.00
Miscellaneous Supplies
Drum Accessories
FILLING FUNNELS
21.5" OJ) $33.10
21.5" OJ>. W/ Flash arrester $121.10
13.5" OJ) $30.35
9" OJ> $7.95
9" OJ> W/ Flash arrester $108.80
Tower Packing
POLYPROPYLENE
1", 0-25 cubic feet $45.00/cubic foot
1", 26-100 cubic feet ,. $42.75/cubic foot
1", 101-500 cubic feet $33.75/cubic foot
2", 0-50 cubic feet $18.65/cubic foot
2", 51-1,000 cubic feet $14.90/cubic foot
2", 1,001-2,000 cubic feet $12.65/cubic foot
3", 0-50 cubic feet $10.90/cubic foot
3", 51-1,500 cubic feet $9.90/cubic foot
3", 1,501-3,500 cubic feet $8.50/cubic foot
1803
-------
APPENDIX C
Chemical Conversion Factors
Constituent*
Calcium
Iron
Magnesium
Potassium
Sodium
Bicarbonate
Carbonate
Chloride
Hydroxide
Nitrate
Phosphate
Sulphate
Calcium bicarbonate
Calcium carbonate
Calcium chloride
Calcium hydroxide
Calcium sulphate
Ferrous bicarbonate
Ferrous carbonate
Ferrous sulphate
Magnesium bicarbonate
Magnesium carbonate
Magnesium chloride
Magnesium hydroxide
Magnesium sulphate
Potassium chloride
Sodium bicarbonate
Sodium carbonate
Sodium chloride
Sodium hydroxide
Soldium nitrate
Sodium phosphate
Sodium sulphate
ing/liter
to
epm
0.0499
0.0358
0.0822
0.0256
0.0435
0.0164
0.0333
0.0282
0.0588
0.0161
0.0316
0.0208
0.0123
0.0200
0.0180
0.0270
0.0147
0.0112
0.0173
0.0132
0.0137
0.0237
0.0210
0.0343
0.0166
0.0134
0.0119
0.0189
0.0171
0.0245
0.0118
0.0183
0.0141
epm
to
mg/llter
20.04
27.92
12.16
39.10
23.00
61.01
30.00
35.46
17.01
62.01
31.67
48.04
81.05
50.04
55.50
37.05
68.07
88.93
57.92
75.96
73.17
42.16
47.62
29.17
60.20
74.56
84.01
53.00
58.46
40.01
85.01
54.67
71.04
gpg
to
epm
0.853
0.612
1.406
0.437
0.743
0.280
0.570
0.482
1.005
0.276
0.540
0.356
0.211
0.342
0.308
0.461
0.251
0.192
0295
0.225
0.234
0.406
0.359
0.586
0.284
0.229
0.203
0.323
0.292
0.427
0201
0.313
0.241
epm
to
gpg
1.172
1.633
0.711
2.286
1.345
3.568
1.754
2.074
0.995
3.626
1.852
2.809
4.740
2.926
3.246
2.167
3.981
5.201
3.387
4.442
4.279
2.465
2.785
1.706
3.520
4.360
4.913
3.099
3.419
2.340
4.971
3.197
4.154
mg/llter to
mg/llter
CaCo,
2.497
1.792
4.115
1.280
2.176
0.820
1.668
1.411
2.926
0.807
1.580
1.042
£"
0.617
1.000
0.902
1.351
0.735
0.563
0.864
0.659
0.684
1.187
1.051
1.715
0.631
0.671
0.596
0.944
0.856
1.251
0.589
0.915
0.704
epm » equivalent parts per million
gpg • grain* per gallon • 17.1 mg/IKer
mg/Hter * milligram* per liter
mg/Hter CaCo, • milligrams per liter of CaCo,
1083
§34
-------
APPENDIXD1
Weight and Measure Equivalencies
Measure of Length
1 Mile = 1,760 yds. - 5,280 ft. = 63,360 Inches
1 Mile = 8 Furlongs = 80 Chains
1 Furlong - 10 Chains = 220 Yds.
1 Chain = 4 Rods = 22 Yds. = 66 Ft. = 100 Links
1 Rod = 5.5 Yds. = 16.5 Ft.
Measure of Length—English to Metric
1 Mile - 1.609 Kilometer
1 Yard = 0.9144 Meter
1 Foot » 0.03048 Meter = 304.8 Millimeters
1 Inch = 2.54 Centimeters = 25.4 Millimeters
Measure of Length—Metric to English
1 Kilometer^0.6214 Mile
1 Meter = 39.37 Inch « 3.2808 Ft. - 1.0936 Yd.
1 Centimeter = 0.3937 Inch
1 Millimeter - 0.03937 Inch
Square Measure
1 Sq. Mile * 640 Acres » 6,400 Sq. Chains
1 Acre » 10 Sq. Chains = 4,840 Sq. Yds. = 43,560 Sq. Ft.
1 Sq. Chain = 16 Sq. Rods = 484 Sq. Yds. = 4,356 Sq. Ft.
1 Sq. Rod = 30.25 Sq. Yds. « 272.25 Sq. Ft. » 625 Sq. Links
1 Sq. Yd. m 9 Sq. Ft.
1 Sq. Ft.«144 Sq. Inches
An Acre Is equal to a Square 208.7 Feet per Side
Square Measure—English to Metric
1 Sq. Mile « 2.5899 Sq. Kilometers
1 Acre * 0.4047 Hectare • 40.47 Acres
1 Sq. Yard = 0.836 Sq. Meters
1 Sq. Foot • 0.0929 Sq. Meters = 929 Sq. Centimeters
1 Sq. Inch = 6.452 Sq. Centimeters » 645.2 Sq. Millimeters
Square Measure—Metric to English
1 Sq. Kilometer = 0.3861 Sq. Mile • 247.1 Acres
1 Hectare » 2.471 Acres • 107,640 Sq. Ft
1 Acre = 0.0247 Acre « 1,076.4 Sq. Ft.
1 Sq. Meter « 10.764 Sq. Ft. -1.196 Sq. Yd.
1 Sq. Centimeter a 0.155 Sq. Inch
1 Sq. Millimeter = 0.00155 Sq. Inch
(3-10
-------
APPENDIX D1
Weight and Measure Equivalencies
Cubic Measure
1 Cubic Yd. • 27 Cu. Ft.
1 Cubic Ft. B 1,728 Cu. Inches
1 Cord = 128Cu. Ft.
1 Gallon = 0.1137 Cu. Ft. = 231 Cu. Inches
1 Cubic Ft. = 7.48 U.S. Gallons
1 U.S. Gallon = 0.83268 Imperial Gallon
1 Imperial Gallon = 1.2009 U.S. Gallons
Cubic Measure—English to Metric
1 Cubic Yd. •= 0.7646 Cubic Meters
1 Cubic Ft. = 28.316 Liters
1 Cubic Inch = 16.38 Cubic Centimeters
1 U.S. Gallon = 3.785 Liters
1 U.S. Quart = 0.946 Liters
1 U.S. Pint« 0.473 Liters
1 Imperial Gallon = 4.542 Liters
Cubic Measure—Metric to English
1 Cubic Meter » 35.314 Cu. Ft. ° 1.308 Cu. Yd. = 264.2 U.S. Gallons
1 Cubic Centimeter » 0.061 Cu. Inch
1 Liter « 0.0353 Cu. Ft. - 61.023 Cu. Inches
1 Liter * 0.2642 U.S. Gallon - 1.0567 U.S. Quart
Measures of Weight—English and Metric
1 Long Ton * 2,240 Lbs. «= 1016.05 Kilograms
1 Short Ton » 2,000 Lbs. = 907.18 Kilograms
1 Metric Ton - 2204.6 Lbs.
1 Kilogram * 2.2046 Lbs.
1 Lb. = 0.45359 Kilograms
Equivalents of Pressure—English and Metric
1 Lb. per Sq. Inch - 0.0703 Kg. per Sq. Centimeter
1 Kg. per Sq. Centimeter » 14.244 Lbs. per Sq. Inch
Weights of Diesel Fuel
1 U.S. Gallon « 7 Ibs. average.
1 U.S. Gallon • 3.17 kilograms.
1903
-------
APPENDIX D2
Energy Equivalencies
Unit
British thermal unit
foot-pound
horsepower-hour
joules
calorie
kilowat-hour
Equivalent"
British thermal
unit
1
1.285x10-*
2,545
9.481 x 10"
3.968 x 10*
3.413
foot-pound
777.9
1
1.98x10*
0.7376
3.087
2.655 X 10*
horsepower-
hour
3.929 x 10"
5.051 x 10'7
1
3.725 x10-7
1.559X10*
1.341
joules
1,055
1.356
2.685 X 10*
1
4.186
3.6 x 10*
calorie
252
0.3239
6.414x10'
0.2389
1
8.601 x 10*
kilowatt-hour
2.93 x 10"
3.766 x 10'7
0.7457
2.778 X10'7
1.163 X1Q-*
1
APPENDIX D3
Mechanical-Electrical Equivalencies
Power
1 horsepower (hp)
1 horsepower-second (hp-sec)
1 horsepower-minute (hp-min)
1 horsepower-hour (hp-hr)
1 horsepower (hp)
550 foot-pounds (ft.-lb.) per second (sec)
33,000 ft.-lb. per minute (min.)
1,980,000 ft.-lbs. per hour (hr.)
.275 ft.-tons per sec.
16.5 ft.-tons per min.
990 ft.-tons per. hr.
550 tt.-lb.
.275 ft.-tons
33,000 tt.-lb.
16.5 ft.-tons
1,980,000 ft.-lb.
990 ft.-tons
746 watts (w)
.746 kilowatts (kw)
1 horsepower-hour
1 Kilowatt-hour
1 Ib. per sq. in.
1 in. of mercury
1 in. of water
Energy
= 2,544 BTU
« .746 KW-hr.
= 3,413 BTU
Pressure
2.0360* of mercury at 32° F.
27.71'of water at 32° F.
2.3091ft. of water at 60° F.
14415. persq. ft.
.491 Ib. per sq. in.
5.2 Ib. per sq. ft.
.0361 Ib. per sq. in.
(3.12
1903
-------
APPENDIX E
Power Required for Pumping
Gals per
Mln.
5
10
15
20
25
30
35
40
45
50
60
70
80
90
100
125
150
175
200
250
300
350
400
500
Theoretical Horsepower Required to Raise Water (at 60 F)
To Different Heights
5ft.
0.006
0.013
0.019
0.025
0.032
0.038
0.044
0.051
0.057
0.063
0.076
0.088
0.101
0.114
0.126
0.158
0.190
0.221
0253
0.316
0.379
0.442
0.505
0.632
10ft.
0.013
0.025
0.038
0.051
0.063
0.076
0.088
0.101
0.114
0.126
0.152
0.177
0.202
0.227
0253
0.316
0.379
0.442
0.505
0.632
0.758
0.884
1.011
1263
15ft.
0.019
0.038
0.057
0.076
0.095
0.114
0.133
0.152
0.171
0.190
0227
0265
0.303
0.341
0.379
0.474
0.568
6.663
0.758
0.947
1.137
1.326
1.516
1.895
20ft.
0.025
0.051
0.076
0.101
0.126
0.152
0.177
0202
0.227
0253
0.303
0.354
0.404
0.455
0.505
0.632
0.758
0.884
1.011
1263
1.516
1.768
2.021
2.526
25 ft.
0.032
0.063
0.095
0.126
0.158
0.190
0.221
0.253
0.284
0.316
0.379
0.442
0.505
0.568
0.632
0.790
0.947
1.105
1263
1.579
1.895
2211
2.526
3.158
30ft.
0.038
0.076
0.114
0.152
0.190
0.227
0.265
0.303
0.341
0.379
0.455
0.531
0.606
0.682
0.758
0.947
1.137
1.326
1.516
1.895
2274
2.653
3.032
3.790
35ft.
0.044
0.088
0.133
0.177
0.221
0.265
0.310
0.354
0.398
0.442
0.531
0.619
0.707
0.796
0.884
1.105
1.326
1.547
1.768
2211
2.653
3.095
3.537
4.421
40ft.
0.051
0.101
0.152
0.202
0.253
0.303
0.354
0.404
0.455
0.505
0.606
0.707
0.808
0.910
1.011
1263
1.516
1.768
2.021
2.526
3.032
3.537
4.042
5.053
45ft.
0.057
0.114
0.171
0.227
0.284
0.341
0.398
0.455
0.512
0.568
0.682
0.796
1.910
1.023
1.137
1.421
1.705
1.990
2274
2.842
3.411
3.979
4.548
5.684
50ft
0.063
0.126
0.190
0.253
0.316
0.379
0.442
0.505
0.568
0.632
0.758
0.884
1.011
1.137
1263
1.579
1.895
2.211
2.526
3.158
3.790
4.421
5.053
6.316
60ft.
0.076
0.152
0.227
0.303
0.379
0.531
0.531
0.606
0.682
0.758
0.910
1.061
1.213
1.364
1.516
1.895
2274
2.653
3.032
3.790
4.548
5.305
6.063
7.579
70ft.
0.088
0.177
0.265
0.354
0.442
0.531
0.619
0.707
0.796
0.884
1.061
1.238
1.415
1.592
1.768
2.211
2.653
3.095
3.537
4.421
5.305
6.190
7.074
8.842
Note: For fluid* other than wate; multiply table valuM by specific gravity. In pumping (quids with a viscosity considerably higher than that of watei; the
pump capacity and head an> reduced. 16 Calcutta the horsepower tor such fluids, pipe friction head must be added to the elevation head to obtain the
total head.
IMS
13-13
-------
APPENDIX E
Power Required for Pumping
Gals per
Mln.
5
10
15
20
25
30
35
40
45
50
60
70
60
90
100
125
150
175
200
250
300
350
400
500
Theoretical Horsepower Required to Raise Water (at 60 F)
To Different Heights
80 tth
0.101
0.202
0.303
0.404
0.505
0.606
0.707
0.808
0.910
1.011
1213
1.415
1.617
1.819
2.021
2.526
3.032
3.537
4.042
5.053
6.063
7.074
8.084
10.11
90ft
0.114
0.227
0.341
0.455
0.568
0.682
0.796
0.910
1.023
1.137
1.364
1.592
1.819
2.046
2274
2.842
3.411
3.979
4.548
5.684
6.821
7.958
9.095
11.37
100ft
0.126
0.253
0.379
0.505
0.632
0.758
0.884
1.011
1.137
1.263
1.516
1.768
2.021
2.274
2.526
3.158
3.790
4.421
5.053
6.316
7.579
8.842
10.11
12.63
125ft
0.158
0.316
0.474
0.632
0.790
0.947
1.105
1.163
1.421
1.579
1.895
2211
2.526
2.842
3.158
3.948
4.737
5.527
6.316
7.895
9.474
11.05
12.63
15.79
150ft
0.190
0.379
0.568
0.758
0.947
1.137
1.326
1.516
1.705
1.895
2274
2.653
3.302
3.411
3.790
4.737
5.684
6.632
7579
9.474
11.37
1326
15.16
18.95
175ft
0.221
0.442
0.663
0.884
1.105
1.326
1.547
1.768
1.990
2211
2.653
3.095
3.537
3.979
4.421
5.527
6.632
7.737
8.842
11.05
13.26
15.47
17.68
22.11
200ft
0.253
0.505
0.758
1.011
1.263
1.516
1.768
2.021
2274
2256
3.032
3.357
4.042
4.548
5.053
6.316
7.759
8.842
10.11
12.63
15.16
17.68
2021
2526
250ft
0.316
0.632
0.947
1263
1.579
1.895
2.211
2.526
2.842
3.158
3.790
4.421
5.053
5.684
6.316
7.895
9.474
11.05
12.63
15.79
18.95
22.11
2526
31.58
300ft
0.379
0.758
1.137
1.516
1.895
2274
2.653
3.032
3.411
3.790
4.548
5.305
6.063
6.821
7.579
9.474
11.37
13.26
15.16
18.95
22.74
26.53
30.32
37.90
350ft
0.442
0.884
1.326
1.768
2211
2.653
3.095
3.537
3.979
4.421
5.305
6.190
7.074
7.958
8.842
11.05
13.26
15.47
17.68
22.11
26.53
30.95
35.37
4421
400ft
0.505
1.011
1.516
2.021
2.526
3.032
3.537
4.042
4.548
5.053
6.063
7.074
8.084
9.095
10.11
12.63
15.16
17.68
2021
2526
30.32
35.37
40.42
50.53
Not*: For flukto otter than watat; multiply taWa vatoaa by •pacific gravty. In pumping Iqulds wtth • vboostty conaldambly hlghar than that of wttat
tha pump capacity and head art raduoad. To calculate tha homepowar tor auch flutta. plpa friction hoad mint oa addad to tha etavatton haad to obtain
tha total haad.
JM4
1983
-------
APPENDIX F
Variables for Pumping Applications
Effect of Speed and Impeller Diameter on Centrifugal Pumps
Within certain limitations, there are three rules governing the operation of centrifugal pumps:
1. Capacity increases proportionately as the speed or the impeller diameter increases.
2. Head varies as the square of the speed or the square of the impeller diameter.
3. Power varies as the cube of the speed or the cube of the impeller diameter.
Atmospheric Pressure
Atmospheric pressure at sea level is approximately 14.7 pounds per square inch. This pressure with a perfect
vacuum will maintain a column of mercury 29.9 inches high or a column of water 33.9 feet high. Neglecting
vapor pressure of the water (see the section on pumping warm water, page 10), this is the theoretical height to
which water may be drawn by suction. The practical limit to which cold water (60'F.) can be drawn by suction at
sea level is 25 ft., and common sense dictates that the suction line should be kept just as short as the
circumstances will permit. It should be understood that it is the pressure or weight of the air that pushes the
water up the suction line. In addition, this air pressure must impart velocity to the water to get it into the pump
and must overcome the friction resulting from the flow of water in the suction line. Thus, the lower the suction
lift, the greater will be the percentage of the air pressure that is available for imparting velocity to the water and
overcoming the suction line friction. For this reason, the lower the suction lift, the more water the pump will get.
Flow of Liquid in Pipe or Hose
Horsepower Formula
One horsepower = 33,000 ft.-lbs. per minute
theoretical liquid horsepower = GPM x total head (feet) x sp. gr.
3,960
theoretical water horsepower * GPM x total head (feet)
3,960
GPM x IDS, per sq. In.
1,715
brake horsepower * theoretical water horsepower
pump efficiency
To determine the area of the required pipe to discharge a given volume (gallons) In a fixed time (minutes) at a
given velocity:
velocity (ft/sec) = GPM x .408 = .321 x GPM
(dia. In Inches') Area (sq. in.)
pipe area (sq. in.) = .321 x gallons
TxVel. (ft/sec)
1909 13-15
-------
APPENDIX F
Doubling the diameter of a pipe or cylinder increases its capacity four times. For the same diameter, friction of
liquids in pipe or hose increases approximately as the square of the velocity.
Pumping Warm Water
For a particular temperature, the actual theoretical height that water can be drawn by suction by a perfect
vacuum at sea level is obtained by subtracting the vapor pressure (in feet) of water at that temperature from
33.9 feet. For example, at room temperature (72T.), this theoretical limit becomes 33 feet, and at 160T., this
limit is 22.9 feet. Since proper allowance must be made for water velocity and friction, the practical limits are
less than the theoretical. If the water is not hot enough, it is necessary to place the pump below the level of the
water so that there is an actual head on the suction. The following chart gives practical suction lifts and suction
heads for pumping water of different temperatures and at different elevations.
Effect of Altitude on Pumps
When a pump is operated at elevations above sea level, the lower atmospheric pressures encountered have a
double effect on the pump performance.
1. The lower atmospheric pressure cannot support as high a column of water so that the maximum practical
suction lift decreases.
2. The lower atmospheric pressure reduces the horsepower output of the gas engine, thus causing It to lose
speed which results In a loss of capacity and discharge head of the pump.
At elevations above sea level, the suction lift on the pump should be reduced accordingly to insure that the
same amount of water can get into the pump as would get in at the equivalent sea level lift. The following table
gives equivalent suction lifts for various elevations.
13-16
1999
-------
APPENDIX F
Equivalent Suction Lifts for Various Elevations
Attitude Suction Lifts in Feet
Sea Level 10.0 15.0 20.0 25.0
2,000ft. 8.8 13.2 17.6 22.0
4,000 ft. 7.8 11.7 15.6 19.5
6,000ft. 6.9 10.4 13.8 17.3
8,000ft. 6.2 9.3 12.4 15.5
10,000ft. 5.7 8.6 11.4 14.3
When a gas engine driven pump is operated at elevations of 4,000 ft. or over, the engine should be equipped
with a high altitude head. However, even with a special cylinder, there is still a power loss of approximately
3% for every 1,000 ft. of elevation. This will result in a loss of speed and a loss of pump performances. The
following table gives the loss in performance that can be expected at various elevations.
Loss of Performance at Various Elevations
Altitude Discharge Head
Sea Level 100% 100%
2,000ft. 97% 95%
4,000ft. 95% 91%
6,000 ft. 93% 87%
8,000ft. 91% 83%
10,000 ft. 88% 78%
1983 §3-17
-------
COST GUIDE
FOR
REMEDIATION EQUIPMENT
AT
UST SITES
§4, GLOSSARY
JULY 1993
-------
GLOSSARY
Activated Carbon: A granular material produced by the roasting of cellulose base
substances, such as wood or coconut shells, in the absence of air. It has an extremely
porous structure and is highly adsorbent; H is used to remove organic matter and certain
dissolved gases from contaminated groundwater.
Aeration: The process of bringing air into contact with water, usually by bubbling air
through the water to remove dissolved gases.
Air Sparging: A process that involves injecting air under pressure below the surface of
groundwater Onto the saturated zone) to produce bubbles that rise and carry dissolved
volatile contaminants from the groundwater into unsaturated soils above. These volatile
contaminants may then be removed from the soils using a vapor extraction system.
Air Stripping: A process in which air and contaminated water are brought into contact in
an engineered unit to allow the volatile contaminants to diffuse from the water into the air.
Annulus: The space between the drill string or casing and the wall of the borehole or
outer casing.
Backwash: The process in which filter beds are subjected to water flow opposite to the
service flow direction to loosen the bed and flush solid materials accumulated on the resin
bed to waste.
Baghouses: Dust collection device used primarily in soil treatment, such as low
temperature thermal desorption. Air flows into the baghouse and is distributed across the
"bags," which are fabric filters that allow for filtration of the air stream.
Barite: Natural finely ground barium sulfate used for increasing the density of drilling
fluids.
Bedrock: A general term for the rock, usually solid, that underlies soil or other
unconsolidated material.
Bentonite: A colloidal clay, usually made up of the mineral sodium montmorillonite.
BioreactoR A vessel constructed specifically to promote the growth of microorganisms
that can degrade the contaminants dissolved in the groundwater. Such factors as oxygen
levels, temperature, and nutrient levels can be controlled to optimize the efficiency whh
which microorganisms degrade the contaminants.
Bladder Pumps: Also known as squeeze pumps, bladder pumps operate by the
compression of a flexible bladder housed inside the pump. Water enters the bladder
1983 §4-1
-------
L
drawa Mpwiurd by sapfflssy fores.
Ad!s®iripilD©na = Vajj»®irs Hh@ MS© of asSivsted ^Aoa (mnasiy
-------
GLOSSARY
transfer pumps to move liquid from one storage area, such as a sump, to another. See
also, Electric Submersible Pumps.
Chemical Metering Pumps: Used to measure the rate at which nutrients are introduced
into bioreactors. Chemical metering pumps operate through a positive displacement piston
which, through tight housing tolerances, creates suction on the intake and then forces the
fluid (or gas) through the outlet port on the downstroke.
Colloid: Extremely small solid particles, 0.0001 to 1 micron in size, which will not settle
out of a solution; intermediate between a true dissolved particle and a suspended solid
which will settle out of solution.
Cone of Depression: A depression in the groundwater table that has the shape of an
inverted cone and develops around a well from which water is being withdrawn. It defines
the area of influence of a well.
Diaphragm Pumps: Diaphragm pumps are used to pump fluids that may contain
sediment or other granular material that could damage a centrifugal pump and its impeller.
Diaphragm pumps operate with two check valves separated by a diaphragm that moves up
and down, creating pressure and suction in the same manner as a piston. As suction is
created, one check valve is lifted off its seat while the other is pulled against hs seat,
allowing for water to flow into a chamber. As the diaphragm comes down, the first valve
reseats and the second is pushed off hs seat, allowing the water to flow out of the chamber
and through the system.
Downhole Filter-Separators: Used to remove hydrocarbons from groundwater, filter-
separators employ an oleophilic (oil-absorbing) - hydrophobic (water-repelling) filter
which allows hydrocarbons to enter a collection chamber but repels water. Recovered
product typically has less water mixed in with h than when using downhole skimmers.
Filter separators also permh the effective recovery of free product when the water table is
fluctuating significantly.
Drawdown: The distance between the static water level and the surface of the cone of
depression.
Drill Collar: A length of extremely heavy steel tube. It is placed in the drill string
immediately above the drill bit to !*v"in"7^ bending caused by the weight of the drill pipe.
Drilling fluid: A fluid used in well drilling operations to remove cuttings from the hole,
to dean and cool the bit, to reduce friction between the drill string and the sides of the
hole, and to seal the borehole.
1908 §4-3
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GLOSSARY
Drum Deheaders: Essentially large can openers, drum deheaders are tools for cutting off
the tops of drums. Powered units and manual units are available to cut both inside and
outside the chime, depending on the need to reuse the drum.
Effluent: A waste liquid byproduct from a manufacturing or treatment process, in hs
natural state or partially or completely treated, that is discharged into the environment.
Electric Submersible Pumps: Electric submersible pumps are used for purging and
dewatering of wells and, more recently, for sampling of monitor wells. Because the
pumps are capable of being submerged in wells, the pump's energy can be fully devoted to
moving the water up instead of to creating a vacuum to prime the pump. Electric
submersible pumps utilize impellers to create centrifugal force that creates the water flow
in and out of the pump housing.
Filter Cake: The suspended solids that become deposited on a porous medium as a
solution is filtered.
Filter Pack: Sand or gravel that is smooth, uniform, clean, well-rounded, and siliceous. It
is placed in the annulus of the well between the borehole wall and the well screen to
prevent geologic formation material from entering the screen.
Fixed Film Bioreactors: Enclosed chamber with fixed surfaces for the growth of
bacteria, a pumping system for the throughput of contaminated water, and an inlet for
nutrients required for bacterial cultures. The contaminated water is filtered through the
bacteria which digest the hydrocarbons.
Flocculation: The agglomeration of finely divided suspended solids into larger, usually
gelatinous, particles; the development of a "floe" after treatment with a coagulant by
gentle stirring or mixing.
Foaming Agent: See surfactant.
Formation Stabilizer: Sand or gravel placed in the annulus of a wefl between the
borehole wall and the well screen to provide temporary or long-term support for the
borehole.
Fouling: The accumulation of undesirable foreign matter in filtration media, such as in a
packed tower or an ion exchanger, which results in inhibited or retarded flow through the
media or reduced operational efficiency of the packed tower or ion exchanger.
Groundwater Table: The surface between the zone of saturation and the zone of
aeration; the surface of an unconfined aquifer.
§44 1803
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GLOSSARY
Grout: A mixture of cement and water used to fill spaces. Various additives, such as
sand, bentonite, and/or hydrated lime, may be included in the mixture to meet certain
requirements.
Grouting: The placing of grout between the casing and sides of a well bore to a
predetermined height above the bottom of the well. This process secures the casing in
place and excludes water and other fluids from entering the well bore.
Head: Energy contained in a water mass, produced by the water's elevation, pressure, or
velocity.
Hydration: The taking up of water by a substance through absorption and/or adsorption.
Interference: The condition occurring when the area of influence of a water well comes
into contact with or overlaps that of a neighboring well, as when two wells are pumping
from the same aquifer or are located near each other.
Kelly: Hollow steel bar to which power is directly transmitted from a rotary table; its
purpose is to rotate the drill pipe and bit.
Leachate: Liquid that has percolated through and dissolved soluble components of solid
waste.
Low Profile Difluser Aerators: Mechanically simple aeration devices used for treating
water contaminated with VOCs. The devices are comprised of holding tanks that are
frequently separated into compartments by baffles, and a series of difiusers running along
the bottom of the tanks. (A diffuser is a device that reduces the velocity of, and increases
the static pressure of, a fluid or gas passing through a system.) As contaminated water
flows into each compartment of the tank, h is aerated by air pumped through the difiusers,
effecting mass transfer and stripping the VOCs. The water flows out of the system in a
finished state, and the VOC-contaminated vapor is captured and sent to a vapor treatment
system, usually an oxidizer or carbon treatment vessel
Low Profile Tray Aerators: Used for treating water contaminated with VOCs. Similar
to packed towers, low-profile tray aerators employ a series of trays stacked on top of each
other. Each tray has small holes in it that allow pressurized air to flow upward through
the holes in the trays and into a stream of contaminated water, creating aeration and
enhancing transfer of the VOCs out of the water. The VOC-contaminated vapor flows
into a vapor treatment system, such as an oxidizer or a carbon treatment station.
Low Temperature Thermal Desorption Systems: A soil remediation technique in which
contaminated soils are heated at relatively modest temperatures (200 to 500 degrees C),
1993 §4-5
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GLOSSARY
typically within a treatment unit, using direct heat, heated air, or steam to volatilize
organic constituents and separate them from the soils. The separated or desorbed organic
compounds are subsequently collected in a vacuum, then treated or destroyed by a variety
of processes.
Oil Skimmers - Downhole: Used to remove free-floating hydrocarbon product from the
surface of groundwater by skimming. Downhole skimmers are inserted by line into a well
and skim free floating hydrocarbons from the top of the water table through the use of a
traveling buoy and screen that move with the fluctuation of the water table. When the
skimmer has collected its capacity of hydrocarbon, it is emptied by pumping the collected
product to a surface storage bin or oil water separator.
Oil/Water Separators: Closed boxes used to separate petroleum hydrocarbons from
water. Coalescing plates attract the hydrocarbons, enhancing their separation and
subsequent flotation. Weirs installed in the unit allow the floating hydrocarbons to spill
over into a storage tank, while the water flows under a baffle and out through an effluent
outlet. Depending on the level of contaminant removal required, the separated water
either may be considered fully treated or may need to be piped to a carbon filtration unit
for further treatment. The separated hydrocarbons can frequently be salvaged and reused.
Packed Tower Air Strippers: Used to strip volatile organic compounds from a water
stream. Influent is pumped to the top of the tower where it is diffused or sprayed over the
tower packing. As the water cascades down through the packing material, high pressure
air is blown up from underneath the packing. This aeration of the water results in mass
transfer of the VOCs from liquid-phase to vapor-phase. The water flows down to a sump
in the bottom of the tower, then flows out via either a gravity feed or a pumping system.
The VOC-contaminated vapor is routed to a vapor treatment system, usually an oxidizer
or a carbon treatment station.
Pipe Locators: Battery powered units designed to identify the magnetic field of
underground ferrous and nonferrous objects. See also, Cable Locator*.
Pugmin Mixers: Large paddle mixing units used to mix additives or nutrients into
contaminated soil prior to thermal desorption or bioremediation. Usually electrically
driven by a motor on one end of a tub with a discharge outlet at the other end.
Radius of Influence: The radial distance from the center of a weH bore to the point where
there is no lowering of the water table (the edge of its cone of depression).
Recharge: The addition of water to the zone of saturation; also, the amount of water
added.
144 1M3
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GLOSSARY
Redox: A chemical reaction in which an atom or molecule loses electrons to another atom
or molecule. Also called oxidation-reduction. Oxidation results from a loss of electrons,
while reduction results from a gain in electrons.
Residual Drawdown: The difference between the original static groundwater level and
the depth to groundwater at a given instant during the remediation process.
Rototilltr. Soil mixing device used in land farming. Operated like a lawnmower, it is gas-
or diesel-powered and is used to till earth and/or mix in additives. Ride-on versions
include a small tractor with a turning till either on the rear or mounted in the middle of the
chassis.
Sieve Analysis: Determination of the particle-size distribution of a soil, sediment, or rock
by measuring the percentage of the particles that will pass through standard sieves of
various sizes.
Soil Vapor Extraction Systems: A process in which vacuum extraction wells are used to
induce air flow through unsaturated soils to vaporize and strip any volatile organic
compounds from the soils into induced air streams. The compounds are then captured in
the extraction wells and subsequently vented, or they are treated in a vapor treatment
system.
Static Water Level: The level of water in a weO that is not being affected by withdrawal
of groundwater.
Steam Stripping: An adjunct to soil vapor extraction, steam stripping is the process of
injecting pressurized steam in and around an extraction well's zone of influence. The
steam aids in desorbing organic compounds from soil pores and so functions as an in situ
soil wash or rinse. The steam vapor and moisture, along with any stripped organics, are
then extracted by a soil vapor extraction system. See also, Air Sparging.
Surface Filter-Separators: Typically used in trench and pond recovery, surface fiher-
separators operate in the same manner as downhole types except that they are larger in
diameter and can recover floating product at a faster pace. See also, Downhole Filter-
Separators.
Surfactant: A substance capable of reducing the surface tension of a liquid in which h is
dissolved. Used in air-based drilling fluids to produce foam and during well development
to disaggregate days.
Thermal Oxidizers: High temperature burners used for destroying VOCs in the vapor
phase.
IMS §4-7
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GLOSSARY
Total Dissolved Solids (IDS): The quantity of dissolved material in a sample of water,
usually expressed in milligrams per liter (mg/1). It is either a measure of the residue
produced by the evaporation of the water sample at 356 degrees Fahrenheit, or for waters
that contain more than 1,000 mg/I of dissolved solids, a measure of the sum of the
chemical constituents.
Trench Linen: Impermeable materials used to prevent contaminated water from
percolating back into the soil. Liners are also used as protection in landfills against
contaminants leaching out of the refuse and seeping into the sofl and groundwater. While
usually made of polyethylene, other materials, such as compacted bentonite, can be used
as liners as well.
Vadose Zone: The zone containing water under pressure less than that of the atmosphere,
including soil water, intermediate vadose water, and capillary water. This zone is bounded
by the surface of the land and the surface of the zone of saturation (the water table).
Volatile Organic Compounds (VOCi): Carbon containing compounds that readily
vaporize (that is, change from a liquid to a gas) at normal temperatures and pressures.
Water Table: The surface between the vadose zone and groundwater, that surface of a
body of unconfined groundwater at which the pressure is equal to that of the atmosphere.
WeD Screen: A filtering device used to keep sediment from entering a water wdL
144 1003
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Introduction
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Equipment
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Appendices
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Glossary
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