EPA-R5-73-023b
July 1973
CAPITAL AND OPERATING COSTS OF
POLLUTION CONTROL EQUIPMENT MODULES
Volume II
Data Manual
by
Herbert G. Blecker
Thomas M. Nichols
Contract No. 68-01-0717
Project 21AQJ
Program Element 1B1030
Project Officer
Dr. Fred H. Abel
Economic Analysis Branch
Implementation Research Division
Prepared for
OFFICE OF RESEARCH AND MONITORING
U.S. ENVIRONMENTAL PROTECTION AGENCY
WASHINGTON, D.C. 20460
-------
EPA Review Notice
This report has been reviewed by the Environmental Protection Agency
and approved for publication. Approval does not signify that the
contents necessarily reflect the views and policies of the Environ-
mental Protection Agency, nor does mention of trade names or commercial
products constitute endorsement or recommendation for use.
ENVIRONMENTAL PROTECTION AGENCY
-------
ABSTRACT
This DATA MANUAL presents, in convenient graphical and tabular form, cost information
for installed equipment item modules on separate data sheets. Each data sheet con-
forms to a uniform style providing information on the specific item and adjustments
to atypical installation, construction, or design.
The methodology used in developing this data and the techniques suggested for its
use are described in detail in the companion User Guide.
This report was submitted in fulfillment of Project Number 21AQJ. Contract Number
68-01-0717, by the ICARUS Corporation, Silver Spring, Maryland, under the sponsor-
ship of the Environmental Protection Agency. Work was completed as of March 1973.
-------
CONTENTS
SECTION PAGE
I Conclusions 1
II Recommendations 2
III Individual Data Sheets 3
IV Acknowledgements 155
V References 156
VI Glossary 157
VII Appendices 158
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SECTION I
CONCLUSIONS
The manual, CAPITAL AND OPERATING COSTS OF POLLUTION CONTROL EQUIPMENT MODULES
(hereafter called ENVIRONMENTAL PROTECTION COST MANUAL), comprising this DATA
MANUAL and companion USER GUIDE enables the user not expertly skilled in the
particular technical field of cost engineering/process economics to prepare
reasonable conceptual cost estimates for proposed environmental protection flow
processing facilities. The easily used graphical and tabular format used for the
presentation of data enable the user to rapidly evaluate alternative cost/process
decisions for proposed environmental protection flow processing facilities.
Using the data in this DATA MANUAL and methods presented in the companion USER
GUIDE, estimates of costs within 10 percent of actual constructed facility costs
were obtained.
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SECTION II
RECOMMENDATIONS
Based upon the results obtained in preparing this ENVIRONMENTAL PROTECTION COST
MANUAL, it is recommended that the following action be taken by the Environmental
Protection Agency:
• The technique of preparing comprehensive cost engineering data using
a computerized detailed estimating system for this ENVIRONMENTAL
PROTECTION COST MANUAL as applied to the installed equipment item
module costs should be extended into the environmental protection
process area. This ENVIRONMENTAL PROTECTION COST MANUAL has directed
its efforts primarily toward the development of comprehensive cost
engineering data on individual installed equipment item module costs
which can be cumulatively developed into a proposed environmental
protection flow processing facility cost. This same technique can be
applied in developing overall process costs as a function of effluent
guideline, regional location, etc.
• A procedure should be implemented so that the data in the DATA MANUAL
is updated on a bi-annual basis. The cost engineering relationships
in the DATA MANUAL are based upon 1972 technology. Technology in the
construction industry is rapidly changing and it is recommended that
these changes be tracked by bi-annual updates to the DATA MANUAL.
• Training courses in the utilization of the cost engineering information
and methods presented in this MANUAL should be implemented and offered
to technical personnel evaluating this type of information at the
regional and headquarters level.
• The DATA MANUAL should be expanded to include additional installed
equipment item module costs representing the new pollution control
technology developed during the course of the development of the DATA
MANUAL but not considered in the initial contract.
-------
SECTION III
INDIVIDUAL DATA SHEETS
-------
AIR COMPRESSOR
cr
3
_i
o
Q
C-J
CTl
co
o
Q
LJJ
100
BRAKE HORSEPOWER (HP)
1000
AC-1
AIR COMPRESSOR
10000
1000000
100000
10000
100
1000
INLET CAPACITY (CFM)
10000
DESIGN ADJUSTMENT
Curve
Type
One Stage Single Reciprocating C
Two Stage Single Reciprocating C
Three Stage Single Reciprocating C
Two Stage Duplex Reciprocating B
Motor Driven Centrifugal
Turbine Driven Centrifugal
Gas Engine Driven Reciprocating
D
Capacity
Range
1.000 100-1800 CFM
1.561 100-1800 CFM
3.440 100-1800 CFM
1.000 600-9000 CFM
1.000 200-3000 BHP
0.870 200-3000 BHP
1.190 200-3000 BHP
Pressure
Rating
(PSIG)
150
500
2500
125
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
R
1.000
1.053
0.070
029
081
026
,047
.029
.055
1.024
-------
AC-2
AIR COMPRESSOR
Installed air compressor cost includes purchased cost of air compressor, base plate,
coupling, driver, cooler, handling and setting, piping, concrete, steel, instrumenta-
tion, electrical, insulation, paint, and indirect costs (prime contractor engineering
and construction overhead).
INSTALLED AIR COMPRESSOR COST,$ = (INSTALLED BASE COST) (Fn)(F0)
JJ K
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.91 to 1.57 percent of installed air compressor
cost.
, OPERATION COST
The air compressor will require between 0.03 and 0.039 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05 - 0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
-------
ACU-1
AIR CONDITIONING UNIT
10
100000
AIR CONDITIONING UNIT
CAPACITY (TONS)
100 1000
o
Q
CN
t-^
01
10000
M
O
£
tn
Type
Roof Mounted
Air Conditioning System
1000
DESIGN ADJUSTMENT
Curve
0.00
0.00
OTHER COST DATA
Type
Floor Mounted
Window Vented
Installed Base Cost
(1972 Dollars)
815.00
1220.00
10
CAPACITY (HP)
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
10
000
,102
0. 989
1.054
1. 097
1.039
1.084
1.050
1.079
1.052
100
-------
ACU-2
AIR CONDITIONING UNIT
Installed air conditioning unit cost includes purchased cost of air conditioning unit,
handling and setting, piping and ductwork, concrete, steel, instrumentation, electrical,
insulation, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED AIR CONDITIONING UNIT COST.$ = (INSTALLED BASE COST) (F- + FD)
U K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.5 percent of installed air conditioning
unit cost.
OPERATION COST
Air conditioning units require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
-------
AD-1
AIR DRYER
AIR DRYER
Of.
3
_j
o
Q
CM
O1
o
o
1000000
100000
10000
100
1000
CAPACITY (CFM)
10000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
9
10
R
1.000
1.010
0.938
1.024
1.121
031
044
054
050
1.010
-------
AD-2
AIR DRYER
Installed air dryer cost includes purchased cost of air dryer, handling and setting,
piping, concrete, steel, instrumentation, insulation, paint, and indirect costs
(prime contractor engineering and construction overhead).
INSTALLED AIR DRYER COST.$ = (INSTALLED BASE COST) (FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.56 percent of installed air dryer cost.
OPERATION COST
Air dryers require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056- .091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
-------
AOT-1
AGITATED OPEN TANK
AGITATED OPEN TANK
1000000
D
cte>
o
Q
Csl
r~^
CTl
8 100000
ca
n
10000
1000
10000
MATERIAL ADJUSTMENT
CAPACITY (GALLONS)
Material
CS
SS304
Al
Ni
Monel
Cu
Moly
Glass Lined CS
1/4 inch Rubber Lined CS
A 204 CS
Ti
M
000
045
750
025
1.924
1.739
2.578
2.827
1.462
504
2.056
REGIONAL ADJUSTMENT
Region Fn
1
2
3
4
5
6
7
8
9
10
000
071
0.979
038
084
029
067
032
072
1.035
1.12
- TEMPERATURE ADJUSTMENT
1.00
500 1000
TEMPERATURE (°F>
10
1500
-------
AOT-2
AGITATED OPEN TANK
Installed agitated open tank cost includes purchased cost of agitated tank, impeller,
motor and drive, handling and setting, piping, concrete, steel, instrumentation,
electrical, insulation, paint, and indirect costs (prime contractor engineering and
construction overhead).
INSTALLED AGITATED OPEN TANK COST,$ = (INSTALLED BASE COST) (FM) (FR) (Fp) (F-,.)
ANNUAL MAINTENANCE
Annual maintenance will vary from 7.38 to 10 percent of installed agitated open tank
cost and will depend primarily upon severity of process conditions (temperature,
cycling, viscosity).
OPERATION COST
Agitated open tanks require between 0.25 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056- .091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
11
-------
APT-1
AGITATED PRESSURE TANK
AGITATED PRESSURE TANK
1000000
o
Q
csi
i-^
at
in
o
u
<
ca
Q
LU
_i
<
100000
DESIGN ADJUSTMENT
10000
100
Type
Autoclave
Mixer
Jacketed
Reactor
ASME Code
Designed
Range
(Gallons)
100-2000
100-10000
100-2000
100-2000
Curve
A
B
A
1.0000
1.0000
0.6635
1.0000
Type
Autoclave
Autoclave
Mixer
Mixer
Mixer
Mixer
Jacketed
Reactor
Jacketed
Reactor
MATERIAL ADJUSTMENT
Material FM
Symbol
CS 0.000
SS304 0.610
CS 0.000
SS304 0.110
SS316 0.117
SS347 0.179
SS304 0.065
Glass Lined CS 0.136
OVERALL CAPACITY (GALLONS)
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
rR
1.000
1.068
0.981
036
078
028
065
031
069
1.034
100
500
1000
1500
PRESSURE (PSIG)
12
-------
APT-2
AGITATED PRESSURE TANK
Installed agitated pressure tank cost includes purchased cost of agitated pressure
tank (autoclaves include design by vendor, thermometer well, blow pipe,full vacuum
rating), motor and drive, skirt, handling and setting, piping, concrete, steel,
instrumentation, electrical, insulation, paint, and indirect costs (prime contractor
engineering and construction overhead).
INSTALLED AGITATED PRESSURE TANK COST.S = (INSTALLED BASE COST) (.Fp + FM + Fp)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 0.883 percent of installed agitated pressure
tank cost and will primarily depend upon process conditions (temperature, pressure,
viscosity, cycling).
OPERATION COST
Agitated pressure tanks require between 0.25 and 1.00 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE
(percent)
Heavy Chemical
Oil and Gas Refining
Resins and Polymers
Food and Beverage
Pulp and Paper
Mining
0.071-0.091
0.063-0.071
0.071-0.111
0.056- .091
0.063-0.100
0.063-0.100
EXPECTED LIFETIME
(years)
11-20
14-16
9-14
11-18
10-16
10-18
13
-------
AS-1
AERATION SYSTEM
AERATION SYSTEM
1000000
100000
10000
_ 10.5 HOURS RETENTION TIME
0.1
1.0
CAPACITY (MGD)
10.0
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
10
000
045
0.947
043
133
041
.066
.065
.067
.029
14
-------
AS-2
AERATION SYSTEM
Installed aeration system cost includes reinforced concrete basin, floating
mechanical aerators, piping, concrete, steel, instrumentation, electrical,
paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED AERATION SYSTEM COST,$ = (INSTALLED BASE COST)(FD)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 0.5 to 1.5 percent of installed aeration
system cost.
OPERATION COST
Aeration systems require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIEFTIME
(percent) (years)
Heavy Chemical 0.016 - 0.040 25-60
Oil and Gas Refining 0.016 - 0.040 25-60
Resins and Polymers 0.016 - 0.040 25-60
Food and Beverage 0.016 - 0.040 25-60
Pulp and Paper 0.016 - 0.040 25-60
Mining 0.016 - 0.040 25-60
15
-------
BLENDER
BL-1
BLENDER
100000
o
o
u> 10000
1000
10
100
POWER (HP)
CAPACITY (CUBIC FEET)
Type
DESIGN ADJUSTMENT
Curve
Rotary A
Spiral Ribbon B
1.000
1.000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
R
.000
.036
,943
.036
1.131
1.037
1.051
1.059
1.063
1.022
16
-------
BL-2
BLENDER
Installed blender cost includes purchased cost of blender, motor and drive, handling
and setting, piping and ductwork, concrete, instrumentationt electrical, paint, and
indirect costs (prime contractor engineering and construction overhead),
INSTALLED BLENDER COST,$ = (INSTALLED BASE COST)(FD>(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.3 percent of installed blender cost and
will primarily depend upon cycling, product characteristics and batch time.
OPERATION COST
Blenders require between 0.125 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10^18
17
-------
C-l
CONDENSER
CONDENSER
100000
o
Q
UJ
CO
<
£
CO
10000
1000
10
100
WATER RATE (GPft)
1000
MATERIAL ADJUSTMENT
Material F.
M
CI
CS
Rubber Lined CS
1.000
0.779
1.209
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
000
068
0.981
034
079
026
062
025
070
1.031
18
-------
C-2
CONDENSER
Installed condenser cost includes purchased cost of barometric condenser, handling and
setting, piping, concrete steel, instrumentation, electrical, insulation, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED CONDENSER COST,$ = (INSTALLED BASE COST)(FM) (FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.75 to 0.90 percent of installed condenser cost and
will depend upon severity of process conditions.
OPERATION COST
Condensers require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056- .083 12-18
Pulp and Paper 0.063 16
Mining 0.063-0.100 10-18
19
-------
CE-1
CRANE
CRANE
1000000
trt
a:
5
o
a
CSI
en
g 100000
<£
O)
10000
10
CAPACITY (TONS)
100
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
R
000
040
0.995
022
040
036
027
018
031
1.018
20
-------
CE-2
CRANE
Installed crane cost includes purchased cost of crane, field erection, steel, electrical,
paint, and indirect costs (prime contractor engineering and construction overhead).
INSTALLED CRANE COST.* = (INSTALLED BASE COST) (F0)
K
ANNUAL MAINTENANCE
Annual maintenance will vary from 2.11 to 2.14 of installed crane cost.
OPERATION COST
Cranes require no operator attention.
INPUSTRY GROUP
Heavy Chemical
Oil and Gas Refining
Resins and Polymers
Food and Beverage
Pulp and Paper
Mining
PROBABLE ANjNUAL DEPRECIATION RATE
DEPRECIATION RATE
(percent)
0.05-0.091
0.063-0.071
0.071-0.111
0.056-0,091
0.063-»0.100
0.063-0.100
EXPECTED LIFETIME
(years)
11-20
14-16
9-14
11-18
10-16
10-18
21
-------
CO-1
CONVEYOR
1000000
o
Q
CM
P-,
CD
<
-------
CO-2
CONVEYOR
Installed conveyor cost includes purchased cost of conveyor, motor, and drive,
handling and setting, ductwork, concrete, instrumentation, electrical, paint,
and indirect costs (prime contractor engineering and construction overhead).
INSTALLED CONVEYOR COST,$ = (INSTALLED BASE COST)(FD)(Fn)
K JJ
ANNUAL MAINTENANCE
Annual maintenance will vary from .32 to 6.85 percent of installed conveyor cost
and will depend upon abrasiveness and particle size of material being transported.
OPERATION COST
Conveyors require no operator attention. Operator attention is determined at
processing functions at either end of conveyor.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.071 14-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
23
-------
CO-3
APRON CONVEYOR
ARROW CONVEYOR
1000000
in
at
TI
s
S
i*
in
!Z
100000
10000
10
LENGTH (FEET)
100
REGIONAL ADJUSTMENT
Region F
9
10
R
000
037
0.959
027
100
027
042
045
050
1.019
24
-------
CO-4
APRON CONVEYOR
Installed apron conveyor cost includes purchased cost of apron conveyor, motor and
drive, handling and setting, ductwork concrete, instrumentation, electrical, paint,
and indirect costs (prime contractor engineering and construction overhead).
INSTALLED APRON CONVEYOR COST.$ = (INSTALLED BASE COST) (FJ
K
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.142 to .265 percent of installed apron conveyor
cost and will depend upon abrasiveness and particle size of material being conveyed.
OPERATION COST
Apron conveyors require no operator attention. Operator attention is determined at
processing steps at either end of conveyor.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.071 14-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
25
-------
CO-5
ROLLER CONVEYOR
ROLLER CONVEYOR
1000
'000000000"
o
Q
Ovl
r^
CD
§
Q
LLI
100
100
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
'R
1.000
1.039
0.967
1.030
1.112
1.028
1.041
1.054
1.049
1.015
1.00
12 13 14 15 16 17 18 19 20 21
WIDTH (INCHES)
26
-------
CO-6
ROLLER CONVEYOR
Installed roller conveyor cost includes purchased cost of roller conveyer, motor and
drive, handling and setting, concrete, instrumentation, electrical, paint, and indirect
costs (prime contractor engineering and construction overhead).
INSTALLED ROLLER CONVEYOR COST.$ = (INSTALLED BASE COST)(Fw)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 6.56 to 6.67 percent of installed roller conveyor
cost and will depend upon usage conditions (cycling, hours per day).
OPERATION COST
Roller conveyors require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.071 14-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
27
-------
CO-7
PNEUMATIC CONVEYING SYSTEM
PNEUMATIC CONVEYING SYSTEM
100000
M
l\ \
05
cc
3
_l
o
Q
CN1
r~v
en
g 10000
a
HI
1000
100
1000
OVERALL SYSTEM LENGTH (FEET)
10000
DESIGN ADJUSTMENT
Pipe Size F
4 inch
3 inch
D
1.000
0.883
REGIONAL ADJUSTMENT
.Region
R
1.000
1.036
0.962
031
106
030
044
048
055
1.020
5 10
FLOWRATfi (T^S/HfO
IS
-------
CO-8
PNEUMATIC CONVEYING SYSTEM
Installed pneumatic conveying system cost includes purchased cost of pneumatic conveying
system components, blower, motor, base, coupling, check valve, filter, field erection,
piping, concrete, steel, instrumentation, electrical, paint, and indirect costs (prime
contractor engineering and construction overhead).
INSTALLED PNEUMATIC CONVEYING SYSTEM COST.$ = (INSTALLED BASE COST)(Fp)(Fp) (FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 7.44 percent of installed pneumatic conveying
system cost and will depend upon hours of operation per day, cycling, fluid abrasiveness
and particle size.
OPERATION COST
The pneumatic conveying system will require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.071 14-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
29
-------
CO-9
BUCKET CONVEYOR
BUCKET CONVEYOR
100000
csi
I-v.
en
CO
o
10000
1000
100
Type
DESIGN ADJUSTMENT
Bucket Size Curve F.,
Centrifugal
Centrifugal
Centrifugal
Centrifugal
Centrifugal
Continuous
Continuous
Continuous
Type
Closed Belt
Closed Belt
Closed Belt
Closed Belt
Open Belt
Open Belt
Open Belt
Open Belt
Bucket
Bucket
Bucket
Bucket
Bucket
Bucket
Bucket
Bucket
6x4
8x5
10 x 6
12 x 7
16 x 8
8x5
14 x 7
15 x 8
Width
(Inches)
36.0
30.0
24.0
18.0
18.0
36.0
42.0
48.0
Curve
A
A
A
A
A
A
A
A
000
163
503
694
007
283
229
6.525
IP.
1.000
0.955
0.889
0.847
0.334
0.696
0.785
0.838
REGIONAL ADJUSTMENT
Region Fp
9
10
1.000
1.036
0.959
1.027
.100
.027
.043
.044
.050
1.018
30
-------
CO-10
BUCKET CONVEYOR
Installed conveyor cost includes purchased cost of conveyor, motor and drive, handling
and setting, ductwork, concrete, instrumentation, electrical, paint, and indirect
costs (prime contractor engineering and construction overhead).
INSTALLED CONVEYOR COST,$ = (INSTALLED BASE COST) (FD)(Fn)
K JJ
ANNUAL MAINTENANCE
Annual maintenance will vary from .32 to 6.85 percent of installed conveyor cost and
will depend upon abrasiveness and particle size of material being transported.
OPERATION COST
Conveyors require no operator attention. Operator attention is determined at processing
functions at either end of conveyor.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.071 14-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
31
-------
CP-1
CENTRIFUGAL PUMP
CENTRIFUGAL PUMP
100000
100000
GPM x HEAD (GPM-FEET)
1000000
10000000
CO
OL
o
o
CNI
I-.*
CT1
UJ
to
S
10000
1000
1000
10000
GPM x HEAD (GPM-FEET)
100000
Material
CS
SS304
Ni
Worthite
Ti
Monel
MATERIAL ADJUSTMENT
F.
M
0.000
0.047
0.107
0.077
0.457
0.101
DESIGN ADJUSTMENT
Fr,
000
101
001
Type
American Voluntary
Standards Heavy Duty
Heavy Duty
Moderate Service
General Service High
Speed Open Impeller 0.950
General Service High Speed 0.976
General Service Medium
Speed Open Impeller 0.942
Turbine Driven Multi
Stage
Motor Driven Multi
Stage
1.190
1.421
REGIONAL ADJUSTMENT
Region F,,
1
2
3
4
5
6
7
8
9
10
000
067
0.978
038
083
026
056
027
068
1.030
32
-------
CP-2
CENTRIFUGAL PUMP
Installed centrifugal pump cost includes purchased cost of centrifugal pump, base plate,
coupling, driver, handling and setting, piping, concrete, instrumentation, electrical,
insulation, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED CENTRIFUGAL PUMP COST.$ = (INSTALLED BASE COST)(FD + FM)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 2.79 to 3.03 of the installed centrifugal pump cost and
will depend upon operational hours per day, pressure, temperature, and fluid abrasiveness.
OPERATION COST
Centrifugal pumps require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
33
-------
CRUSHER
1000000
DRIVER POWER (HP)
100
CR-1
CRUSHER
1000
o
Q
CM
l~^
CD
tn
<
M
Q
UJ
100000
10000
10
100
CAPACITY (TONS/DAY)
1000
DESIGN ADJUSTMENT
Type
Cone Crusher
Gyratory Crusher
Jaw Crusher
Pulverizer
Roll Crusher
Rotary Crusher
Sawtooth Crusher
Curve
A
B
B
B
A
B
A
1.000
1.000
1.092
0.358
1.367
0.744
0.584
REGIONAL ADJUSTMENT
Region FR
1
2
3
4
5
6
7
8
9
10
000
017
0.936
.026
.127
.032
.042
.059
.049
1.012
34
-------
CR-2
CRUSHER
Installed crusher cost includes purchased cost of crusher, handling and setting, ductwork,
concrete, instrumentation, electrical, paint, and indirect costs (prime contractor
engineering and construction overhead).
INSTALLED CRUSHER COST.$ = (INSTALLED BASE COST) (Fn)(FD)
U r\
ANNUAL MAINTENANCE
Annual maintenance will vary from 1,51 to 1.66 percent of the installed crusher cost and be
dependent upon abrasiveness of material being comminuted.
OPERATION COST
Crusher requires between approximately 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.083 12
Pulp and Paper 0.100 10
Mining 0.063-0.100 10-18
35
-------
CRYSTALLIZER
100
1000000
CAPACITY (GALLONS)
1000
CRY-1
CRYSTALLIZER
10000
as
3
o
u
01 100000
s
10000
100
CAPACITY (TONS/DAY)
LENGTH (FEET)
DESIGN ADJUSTMENT
Type Curve
Batch Vacuum A
Forced Circulation B
Mechanical C
Oslo B
REGIONAL ADJUSTMENT
D
0.00
0.00
0.00
0.64
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.043
0.949
041
133
041
064
066
067
1.027
36
-------
CRY-2
CRYSTALLIZER
Installed crystallizer cost includes purchased cost of crystallizer handling and setting,
piping, concrete, steel, instrumentation, electrical, insulation, paint, and indirect
costs (prime contractor engineering and construction overhead).
INSTALLED CRYSTALLIZER COST.S = (INSTALLED BASE COST) (FR + Fp)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.68 to 5.38 percent of the installed crystallizer cost
and will depend upon fluid abrasiveness, temperature, and throughput.
OPERATION COST
Crystallizers require between .16 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.091 11
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056-0.083 12-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
37
-------
CENTRIFUGE
1000000
DIAMETER (INCHES)
10
CT-1
CENTRIFUGE
100
o
Q
CN
i^
CTl
n-f
100000
Ul
_l
_l
<
10000
100
DRIVER POWER (HP)
Type
DESIGN ADJUSTMENT
Curve
ATM Suspended A
Batch Automatic B
Batch Bottom B
Batch Top B
Disk B
Reciprocating Conveyor B
Scroll Conveyor B
Solid Bowl B
Tubular C
Super D B
D
1.000
1.000
0.139
0.165
2.802
2.537
2.095
0.659
1.000
0.630
REGIONAL ADJUSTMENT
Region FF
1
2
3
4
5
6
7
8
9
10
1.000
1.046
0.947
1.042
1.133
1.041
1.064
1.068
1.064
1.029
38
-------
CT-2
CENTRIFUGE
Installed centrifuge cost includes purchased cost of centrifuge, motor and drive, handling
and setting, piping, concrete, steel, instrumentation, electrical, insulation, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED CENTRIFUGE COST,$ = (INSTALLED BASE COST)(Fg)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.326 - 4.39 percent of installed centrifuge cost and
will depend on cycle time, fluid clogging characteristics, temperature and pressure.
OPERATION COST
Centrifuges require between 0.10 and 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
39
-------
CU-1
CUTTER
CUTTER
100000
o
Q
CM
1^
o-i
10000
a
ui
1000
10
POWER (HP)
100
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
R
1.000
1.021
0.931
029
142
036
052
063
058
1.016
40
-------
CU-2
CUTTER
Installed cutter cost includes purchased cost of cutter, motor and drive, handling and
setting, piping, concrete, steel, instrumentation, electrical, paint, and indirect costs
(prime contractor engineering and construction overhead).
INSTALLED CUTTER COST.$ = (INSTALLED BASE COST)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.33 - 1.39 of installed cutter cost and will depend
upon cycle time, material hardness and process throughput.
OPERATION COST
Cutters require between 0 and 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.091 11
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.067-0.091 11-15
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
41
-------
D-l
DRYER
DRYER
CAPACITY (IBS WATER EVAPORATED/HOUR)
1000 10000
LU
in
S
1000
100
AREA (SQUARE FEET)
1000
DESIGN ADJUSTMENT
Type Curves F
D
Atmospheric Tray
Pan
Spray
Vacuum Tray
MATERIAL ADJUSTMENT
Material FM
1.000
3.766
1.000
1.681
REGIONAL ADJUSTMENT
Region F
CS
SS
0.000
0.640
1
2
3
4
5
6
7
8
9
10
R
1.000
1.0S7
0.964
041
111
036
063
053
071
1.033
42
-------
D-2
DRYER
Installed dryer cost includes purchased cost of dryer and accessories (motor and drive
for appropriate types), handling and setting, piping and ductwork, concrete, steel,
instrumentation, electrical, insulation, paint, and indirect costs (prime contractor
engineering and construction overhead).
INSTALLED DRYER COST.$ = (INSTALLED BASE COST) (Fp + FM)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.163 - 2.36 of the installed dryer cost and will depend
upon cycle time, and operating hours per year.
OPERATION COST
Dryers require between 0.2 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.833 12-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
43
-------
DC-1
DUST COLLECTOR
DUST COLLECTOR
100000 I 1
10000 —
1000
1000
CAPACITY (CFM)
DESIGN ADJUSTMENT
Type
D
1.000
0.840
1.213
5.060
Cloth Bay
Centrifugal Precipitator
Cyclone
Electrical Precipitator Hi-Voltage
Electrical Precipitator Low Voltage 3.403
Multiple Cyclone 0.327
Washers 0-967
Automatic Cloth Filter 0.658
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.060
0.982
1.032
1.070
1.024
1.052
1.028
1.056
1.028
44
-------
DC-2
DUST COLLECTOR
Installed dust collector cost includes purchased cost of dust collector (motor and drive for
applicable types) handling and setting, piping and ductwork, concrete, steel, instrumentation,
electrical (if required), insulation, paint, and indirect costs (prime contractor engineering
and construction overhead).
INSTALLED DUST COLLECTOR COST.S = (INSTALLED BASE COST)(Fp)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.40 - 5.37 percent of the installed dust collector and
will depend upon air/media ratio, fluid abrasiveness, particle size, cycle time, and
operating hours per year.
OPERATION COST
Dust collectors require between 0 and 0.05 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
45
-------
DCP-1
DRY CAUSTIC PEELER
DRY CAUSTIC PEELER
1000000
100000
10000
100
CAPACITY (TONS/HOUR)
REGIONAL ADJUSTMENT
Region
I
2
3
4
5
6
7
8
9
10
0.959
,027
.100
,026
041
.044
,050
1.019
46
-------
DCP-2
DRY CAUSTIC PEELER
Installed dry caustic peeler cost includes purchased cost of dry peeler, holding
tank, lye applicator, rinse tank, sprays, flight elevator, troughed conveyor,
pumps, drives, ductwork and chutes, handling and setting, piping, concrete,
steel, instrumentation, electrical, paint, and indirect costs (prime contractor
engineering and construction overhead).
INSTALLED DRY CAUSTIC PEELER COST,$ = (INSTALLED BASE COST)(FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 2 percent of the installed dry caustic
peeler and will be dependent upon cycling and throughput.
OPERATION COST
Dry caustic peelers require between 0.25 and 1.0 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.071 14-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
47
-------
DD-1
DRUM DRYER
DRUM DRYER
1000000
100000
10000
100
AREA (SQUARE FEET)
1000
DESIGN ADJUSTMENT
Type
Double Atmospheric
Single Atmospheric
Single Vacuum
D
1.000
0.909
2.683
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
R
000
,052
965
039
104
,033
,060
.050
,062
1.029
48
-------
DD-2
DRUM DRYER
Installed drum dryer cost includes purchased cost of drum dryer, motor, drive, handling
and setting, piping and ductwork, concrete, steel, instrumentation, electrical, insula-
tion, paint, and indirect costs (prime contractor engineering and construction overhead).
INSTALLED DRUM DRYER COST.$ = (INSTALLED BASE COST) (FD)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.46 - 0.55 percent of installed drum dryer cost and
will depend upon cycle time and operating hours per year.
OPERATION COST
Drum dryers require between 0.2 and O.S operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
49
-------
DW-1
DUCTWORK
DUCTWORK
10000
1000
100
100
1000
TOTAL SURFACE AREA (SQUARE FEET)
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
1.179
50
-------
DW-2
DUCTWORK
Installed ductwork cost includes purchased cost of metal and accessories, handling
and setting, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED DUCTWORK COST/$ = (INSTALLED BASE COST)(Fn)
K
ANNUAL MAINTENANCE
Annual maintenance will vary from 2 to 8 percent of installed ductwork cost and will
primarily depend upon gas/media ratio and fluid abrasiveness.
OPERATION COST
Ductwork requires no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
51
-------
EVAPORATOR
1000000
' A
AREA (SQUARE FEET)
10
E-l
EVAPORATOR
100
CO
cc
<
o
a
100000 -
<
I—
10000
100
1000
10000
AREA (SQUARE FEET)
CAPACITY (GALLONS)
Type
Forced Circulation
Long Tube
Standard Horizontal
Standard Vertical
Jacketed
Long Vertical
Falling Film
DESIGN ADJUSTMENT
Curve P., Base Material
REGIONAL ADJUSTMENT
Region F
A
A
C
A
D
000
1.000
0.617
1.137
1.000
0.318
1.000
1
CS
SS
CS
CS
Glass Lined CS
CS
SS
1
2
3
4
5
6
7
8
9
10
R
1.000
1.074
0.979
036
079
027
071
026
069
1.036
Material
Karbate Tube/CS Shell
Pb Tube/Pb Lined CS Shell
Cu Tube/CI Shell
MATERIAL ADJUSTMENT
Base Material
CS
CS
CS
M
4.458
1.852
0.933
52
-------
E-2
EVAPORATOR
Installed evaporator cost includes purchased cost of evaporator, accessories, handling
and setting, piping, concrete, steel, instrumentation, electrical, insulation, paint,
and indirect costs (prime contractor engineering and construction overhead).
INSTALLED EVAPORATOR COST,$ = (INSTALLED BASE COST) (FD)(FM) (FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.20 - 4.31 percent of the installed evaporator cost
and will depend upon operating hours per year, fluid viscosity, cycle time and tempera-
ture and pressure.
OPERATION COST
Evaporators require between 0.2 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.091 11
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056-0.083 12-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
53
-------
ED-1
ELECTRODIALYSIS
ELECTRODIALYSIS
10000000
1000000
100000
100
1000
CAPACITY (GPM)
10000
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
R
000
022
0.931
039
,152
,045
.062
,077
.062
1.021
54
-------
ED-2
ELECTRODIALYSIS
Installed electrodialysis module cost includes purchased cost of membrane stocks
pumps, and accessories, field erection, piping, concrete, steel, instrumentation,
electrical, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED ELECTRODIALYSIS COST,$ = (INSTALLED BASE COST)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 5 percent of installed electrodialysis
module and will depend upon processing conditions and membrane life.
OPERATION COST
Electrodialysis modules require between 0.25 and 1 operator per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
55
-------
EG-1
ELECTRIC GENERATOR
ELECTRIC GENERATOR
100000
1000,
o
a
csj
r-.
en
o
u
2
Q
10000
100000
Type
DESIGN ADJUSTMENT
Curve FT.
REGIONAL ADJUSTMENT
Portable
Turbo Generator
Unit Steam
A
A
1.000
1.000
2.317
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.001
0.934
.026
,128
.035
.030
.067
,037
1.008
56
-------
EG-2
ELECTRIC GENERATOR
Installed electrical generator cost includes purchased cost of electrical generator,
accessories, handling and setting, interconnecting if required, piping, concrete,
instrumentation, electrical, insulation if required, paint, and indirect costs
(prime contractor engineering and construction overhead).
INSTALLED ELECTRICAL GENERATOR COST,$ = (INSTALLED BASE COST) (Fn)(Fn)
JJ K
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.7 - 2.0 percent of installed electrical generator cost
OPERATION COST
Electrical generators require between 0 and 5 operators per shift depending upon type,
process application and size.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.036 28
Oil and Gas Refining 0.036 28
Resins and Polymers 0.036 28
Food and Beverage 0.036 28
Pulp and Paper 0.036 28
Mining 0.036 28
57
-------
EJECTOR
EJ-1
EJECTOR
100000
3 10000
1000
100
CAPACITY (IBS AIR/HOUR)
1000
DESIGN ADJUSTMENT
Number of Stages F
D
1.00
1.47
3.47
3.90
REGIONAL
Region
1
•J
&
3
4
5
6
7
8
9
10
ADJUSTMENT
FR
1.000
1.084
0.987
1.046
1.081
1.031
1.081
1.033
1.081
1.041
100 200
PRESSURE (MM-HG)
58
300
-------
EJ-2
EJECTOR
Installed ejector cost includes purchased cost of ejector, handling and setting, piping,
steel, insulation, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED EJECTOR COST.$ = (INSTALLED BASE COST)(Fp) (Fp) (FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.6 percent of the installed ejector cost.
OPERATION COST
Ejectors require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
59
-------
EL-1
ELEVATOR
ELEVATOR
1000000
to
ce
3
o
a
100000
o
LU
_i
_i
<
10000
10
DESIGN ADJUSTMENT
Type
Freight
Passenger
1.000
1.506
I
100
LIFT (FEET)
1000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.029
0.996
.014
.026
.008
.011
.011
.020
.011
1,0 2,0 3,0 4,0 5,0 6.0
CAPACITY (TONS)
60
7,0 8,0 9.0
-------
EL-2
ELEVATOR
Installed elevator cost includes purchased cost of elevator, motor and drive, field
erection by subcontractor, structural steel, subcontractors overhead and profit,
indirect costs (prime contractor engineering and construction overhead).
INSTALLED ELEVATOR COST.$ = (INSTALLED BASE COST) (FD)(FC)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.6 percent of installed elevator cost.
OPERATION COST
Elevators require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.016-0.022 45-60
Oil and Gas Refining 0.016-0.022 45-60
Resins and Polymers 0.016-0.022 45-60
Food and Beverage 0.016-0.022 45-60
Pulp and Paper 0.016-0.022 45-60
Mining 0.016-0.022 45-60
61
-------
ES-1
EQUALIZATION SYSTEM
EQUALIZATION SYSTEM
10000000
o
Q
CM
1^
CD
1000000
1.0
CAPACITY (MGPD)
10.0
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
000
045
0.947
1.043
1.133
041
066
065
067
1.029
62
-------
ES-2
EQUALIZATION SYSTEM
Installed equalization system cost includes reinforced concrete basin, variable speed
centifugal pumps, floating aerators, piping, concrete, steel, instrumentation, electri-
cal, paint, and indirect costs (prime contractor engineering and construction overhead)
INSTALLED EQUALIZATION SYSTEM COST,$ = (INSTALLED BASE COST)(FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 0.25 to 0.75 percent of installed equalization
system cost.
OPERATION COST
Equalization systems require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.016-0.040 25-60
Oil and Gas Refining 0.016-0.040 25-60
Resins and Polymers 0.016-0.040 25-60
Food and Beverage 0.016-0.040 25-60
Pulp and Paper 0.016-0.040 25-60
Mining 0.016-0.040 25-60
63
-------
EX-1
EXTRACTOR
EXTRACTOR
1000000
o
Q
CM 100000
t\
CT>
O
CJ
10000
10
CAPACITY (GPM)
100
REGIONAL ADJUSTMENT
Region FR
1
2
3
4
5
6
7
8
9
10
1.000
1.045
0.947
,043
133
,041
,066
,065
,067
1.029
64
-------
EX-2
EXTRACTOR
Installed extractor cost includes purchased cost of continuous centrifugal extractor,
motor and drive, handling and setting, piping, concrete, steel, instrumentation,
electrical, insulation, paint, and indirect costs (prime contractor engineering and
construction overhead) .
INSTALLED EXTRACTOR COST,$ = (INSTALLED BASE COST) (Fn)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 2 percent of the installed extractor cost and
will depend upon cycle time, operating hours per year and process conditions.
OPERATION COST
Extractors require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
65
-------
F-l
FILTER
FILTER
1000000
o
Q
CS1
r^-
CTl
8 100000
10000
B
AREA (SQUARE FEET)
DIAMETER (INCHES)
DESIGN ADJUSTMENT
Type Curve Fr
Sewage
Rotary Drum
Rotary Disk
Plate and Frame
Wet Leaf
Dry Leaf
Sparkler
B
B
B
B
B
B
A
1.00
1.36
1.45
0.25
0.30
0.36
1.00
PLATE AND FRAME
MATERIAL ADJUSTMENT
Material
CS
Pb
Pine
Al
Bronze
SS
1.00
2.15
0.82
1.68
2.91
5.53
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
R
000
,021
0.930
,038
,151
,044
,062
,077
,061
1.021
66
-------
F-2
FILTER
Installed filter cost includes purchased cost of filter, (motor and drive when
applicable), auxiliaries, handling and setting, piping and ductwork, concrete,
steel, instrumentation, electrical, insulation, paint, and indirect costs (prime
contractor engineering and construction overhead).
INSTALLED FILTER COST,$ = (INSTALLED BASE COST)(Fp) (FM)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 3.39 - 5.62 percent of installed filter cost and
will depend upon process thruput, percent solids, particle size, temperature and
pressure, and cycle time.
OPERATION COST
Filters require between 0.25 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
67
-------
FEEDER
100000
05
5
t/>
o
u
ui
-------
FE-2
FEEDER
Installed feeder cost includes purchased cost of feeder, motor and drive, handling and
setting, piping and ductwork, concrete, instrumentation, electrical, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED FEEDER COST,$ = (INSTALLED BASE COST)(Fp)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3 percent of installed feeder cost.
OPERATION COST
Feeders require no operator attention.
>
' PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
69
-------
FL-1
FLAKER
FLAKER
1000000
in
8 100000
1000
AREA (SQUARE FEET)
10000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.050
0.965
038
104
034
059
051
059
1.030
70
-------
FL-2
F LAKER
Installed flaker cost includes purchased cost of flaker, motor and drive, accessories,
handling and setting, piping and ductwork, concrete, steel, instrumentation, electrical,
insulation, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED FLAKER COST.$ = (INSTALLED BASE COST)(FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 2.75 percent of installed flaker cost.
OPERATION COST
Flakers require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
71
-------
FM-1
FLOATATION MACHINE
FLOATATION MACHINE
100000
10000
<
h-
1000
100
CAPACITY (CUBIC FEET)
REGIONAL ADJUSTMENT
Region FR
1
2
3
4
5
6
7
8
9
10
000
050
0.945
044
139
043
071
068
074
1.031
72
-------
FM-2
FLOATATION MACHINE
Installed floatation machine cost includes purchased cost of floatation machine, motor
and drive, handling and setting, piping, concrete, steel, instrumentation, electrical,
insulation, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED FLOATATION MACHINE COST.$ = (INSTALLED BASE COST)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 2 percent of installed floatation machine cost.
OPERATION COST
Floatation machines require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.056-0.100 10-18
Oil and Gas Refining 0.056-0.100 10-18
Resins and Polymers 0.056-0.100 10-18
Food and Beverage 0.056-0.100 10-18
Pulp and Paper 0.056-0.100 10-18
Mining 0.056-0.100 10-18
73
-------
FN-1
FAN
FAN
100000
10000
1000
100
1000
CAPACITY (CFM)
10000
DESIGN ADJUSTMENT
Type
rD
Centrifugal 1.000
Turbo
Centrifugal 32.110
Compressor
Centrifugal 0.106
Propeller 0.063
Rotary 1.692
Blower
Vane Axial 0.134
Pressure
Range
1-30 psig
1000 psig
10 psig
1.0 - 20.0
1.0
1.0
1.0
1.0
1.0
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
R
1.000
1 .047
0.951
1.036
1.125
1.035
1. 054
1.054
1.066
1.025
10.0
1.0
PRESSURE ADJUSTMENT
(CENTRIFUGAL TURBO ONLY) —
A
1.0
10.0
PRESSURE (PSIG)
74
100.0
-------
FN-2
FAN
Installed fan cost includes purchased cost of fan, motor and drive, handling and setting,
piping and ductwork, concrete, steel, instrumentation, electrical, insulation, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED FAN COST,$ = (INSTALLED BASE COST) (FD>(Fp)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.27 - 1.36 percent of installed fan cost.
OPERATION COST
Fans require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
75
-------
FR-1
FREEZER
FREEZER
1000000
U)
3
o
a
CM
01
to
o
o
100000
_1
<
10000
10000
100000
FREEZER (CUBIC FEET)
1000000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
9
10
R
1.000
1.067
0.973
036
091
030
061
035
067
1.031
TEMPERATURE ADJUSTMENT
V-50 40 -30
20 -10 0 KT
TEMPERATURE (°F)
76
~20 33 40
-------
FR-2
FREEZER
Installed freezer cost includes purchased cost of freezer, refrigeration equipment,
structure, field erection by subcontractor, subcontractor overhead and profit, piping,
ductwork, indirect costs (prime contractor engineering and construction overhead).
INSTALLED FREEZER COST,$ = (INSTALLED BASE COST) (Fy) (FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 5 percent of installed freezer cost.
OPERATION COST
Freezers require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.056-0.083 12-18
Oil and Gas Refining 0.056-0.083 12-18
Resins and Polymers O.OS6-0.083 12-18
Food and Beverage 0.056-0.083 12-18
Pulp and Paper O.OS6-0.083 12-18
Mining 0.056-0.083 12-18
77
-------
FU-1
FURNACE
FURNACE
1000000
100000
10000
100
DUTY (MM BTU/HOUR)
DESIGN ADJUSTMENT
Type
Heater
Box
Pyrolysis
Reformer
Vertical
Pressure (PSIG)
1.000
0.890
1.160
1.250
0.670
3000
1000
3000
3000
1000
REGIONAL ADJUSTMENT
MATERIAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
Material
cs
ss
Chrome-Moly
M
1.000
1.264
1.119
1.000
1.041
0.989
027
053
020
,044
026
,043
1.022
78
-------
FU-2
FURNACE
Installed furnace cost includes purchased cost of furnace, field erection by sub-
contractor, blowers, motors and drivers, piping, concrete, instrumentation, electrical,
insulation, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED FURNACE COST.$ = (INSTALLED BASE COST) (FD)(FM)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.7 percent of installed furnace cost.
OPERATION COST
Furnaces require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.083 12-18
Pulp and Paper 0.063 16
Mining 0.100 10
79
-------
GP-1
GEAR PUMP
GEAR PUMP
100000
o
Q
OJ
1-^
CT1
O
O
m
Q
10000
1000
100
CAPACITY (GPM)
1000
DESIGN ADJUSTMENT
Type
D
Canned Rotor 1.000
Mechanical Seal 1.351
(Glass Lined CS only)
REGIONAL ADJUSTMENT
Region FR
1
2
3
4
5
6
7
8
9
10
1.000
1.062
0.982
1.033
.073
.025
.055
.026
.064
1.031
MATERIAL ADJUSTMENT
Material F,.
M
CS
ss
Bronze
0.000
0.175
0.287
80
-------
GP-2
GEAR PUMP
Installed gear pump cost includes purchased cost of gear pump, base plate, coupling,
motor and drive, handling and setting, piping, concrete, instrumentation, electrical,
insulation, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED GEAR PUMP COST.I = (INSTALLED BASE COST) (FD + FM)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.5 - 4.6 percent of installed gear pump cost and
will depend upon cycle time, operating hours per year, fluid abrasiveness, temperature
and pressure.
OPERATION COST
Gear pumps require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
81
-------
HAB-1
HOT AIR BLANCHER
HOT AIR BLANCHER
100000
1000
CAPACITY (BTU/HOUR)
10000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
000
037
959
027
100
027
042
045
050
1.019
82
-------
HAB-2
HOT AIR BLANCHER
Installed hot air blancher cost includes purchased cost of hot air blanching unit,
conveyor belt, driver, gas fired heater, blower, handling and setting, piping,
and ductwork, concrete, steel, instrumentation, electrical, insulation, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED HOT AIR BLANCHER COST,$ = (INSTALLED BASE COST)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.32 to 6.85 percent of installed hot air blancher
cost and will be primarily dependent upon product characteristics and cycling.
OPERATION COST
Hot air blanchers require between O.OS and 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.071 14-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
83
-------
HE-1
HEAT EXCHANGER
HEAT EXCHANGER
1000000,
o
Q
100000
<
Q
1000
AREA (SQUARE FEET)
10000
DESIGN ADJUSTMENT
Design Type
Fixed Tube Sheet
U-Tube Reboiler
Kettle Reboiler
Steam Coil Tank Heater
Jacketed Pipe
Thermascrew (Rietz) Single Screw
Shell and Tube Calandria
Spiral Plate
Thermascrew (Rietz) Twin Screw
Suction Heater
Spiral Tube
Plate Coil - Header Type
Plate Coil - Serpentine Type
Cascade Cooler
Drip Cooler
Fin Tube
Floating Head
U-Tube
Shell f, Tube
Waste Heat Boiler
D
000
010
350
131
561
260
470
060
170
0.638
0. 805
0.977
0.775
0.858
2.940
0.966
0.622
0. 542
1.000
2.180
REGIONAL ADJUSTMENT
Region F
10
R
000
074
0.982
038
087
026
069
027
078
1.037
PRESSURE ADJUSTMENT
500
1000 1500 1900
PRESSURE (PSIG)
-------
HE-2
HEAT EXCHANGER
Tube
Material
CS
SS304
SS304
SS316
Ni
Ni
Ti
Ti
Al
Al
Brass
Brass
Cu
Cu
Monel
Monel
Holy
Holy
Shell
Material
CS
CS
SS304
SS316
CS
Ni
CS
Ti
CS
Al
CS
Brass
CS
Cu
CS
Monel
CS
Moly
MATERIAL ADJUSTMENT
1000 ft
1
1
1
1
1
2
1
2
1
1
1
]
1
1
1
1
2
2
FM
.00
.14
. 22
.34
.66
.01
. 71
.04
.04
.12
.30
.44
.38
.54
.53
.83
.31
.96
10000 ft"
1
1
1
1
1
3
L
3
1
1
1
1
1
J
2
o
L.
3
4
FM
.00
. 24
.43
.67
.82
.14
.62
.10
.18
. 22
.41
.93
. 66
. 93
.03
. 57
.02
.76
Installed heat exchanger cost includes purchased cost of heat exchanger, handling
and setting, piping, concrete, steel, instrumentation, electrical, insulation,
paint, and indirect costs (prime contractor lengineering and construction overhead).
INSTALLED HEAT EXCHANGER COST.S = (INSTALLED BASE COST) (Fp) (Fp) (FM> (FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1 to 2.3 percent of installed heat exchanger cost
and will depend upon fouling characteristics of fluid, temperature and pressure, a?id
fluid velocity.
OPERATION COST
Heat exchangers require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATt
(percent)
Heavy Chemical
Oil and Gas Refining
Resins and Polymers
Eood and Beverage
Pulp and Paper
Mining
0.05-0.091
0.063-0.071
0.071-0.111
0.056-0.091
0.063-0.100
0.063-0.100
EXPECTED LIFETIME
(years)
11-20
14-16
9-14
11-18
10-16
10-18
85
-------
HE-3
ELECTRICAL HEATERS
ELECTRICAL HEATERS
100000
a:
<
o
a
CM
r--.
en
o
o
a
UJ
10000
1000
100
CAPACITY KW
1000
REGIONAL ADJUSTMENT
Region F,n
1
2
3
4
5
6
7
8
9
10
1.000
1.073
0.978
036
083
029
071
027
074
1.035
86
-------
HE-4
ELECTRICAL HEATERS
Installed electrical heater cost includes purchased cost of electrical heater, handling
and setting, piping, concrete, steel, instrumentation, electrical, insulation, paint,
and indirect costs (prime contractor engineering and construction overhead).
INSTALLED ELECTRICAL HEATER COST.$ = (INSTALLED BASE COST) (FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1 to 3 percent of installed electrical heater cost.
OPERATION COST
Electrical heaters require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
87
-------
HO-1
HOIST
HOIST
100000
Q
o
o
CT1
&
<
Q
10000
1000
100
CAPACITY (TONS)
DESIGN ADJUSTMENT
Type F
D
Hoist
Plain Trolly
Gear Trolly
No Trolly
1 Speed
5 Speed
1.000
0.115
0.325
0.089
0.510
0.634
REGIONAL ADJUSTMENT
Region FR
1
2
3
4
5
6
7
8
9
10
1.000
1.040
0.995
.022
,040
.036
.026
.017
.031
1.018
88
-------
HO-2
HOIST
Installed hoist cost includes purchased cost of hoist, field erection, steel,
electrical, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED HOIST COST.S = (INSTALLED BASE COST)(FD)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.28 percent of installed hoist cost.
OPERATION COST
Hoists require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
89
-------
HT-1
HORIZONTAL TANK
HORIZONTAL TANK
1000000
o
Q
100000
10000
1000
10000
CAPACITY (GALLONS)
100000
DESIGN ADJUSTMENT
Type
D
Cylindrical 1.000
Vacuum Receiver 1.000
Jacketed Vacuum 2.830
Receiver
Curve
MATERIAL ADJUSTMENT
Material
CS
Al
Ti
Monel
Ni
Glass Lined CS
Cu
Moly
SS304
SS316
A 204 CS
rM
000
361
449
280
1.342
1.879
1.237
1.599
1.068
1.112
1.006
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
R
1.000
1.062
0.986
,032
,071
.026
.062
026
,069
1.031
1.12
1.08
1.04
1.00
TEMPERATURE ADJUSTMENT -
r
500 1000
TEMPERATURE (°p)
1500
90
-------
HT-2
HORIZONTAL TANK
Installed horizontal tank cost includes purchased cost of horizontal tank, handling
and setting, piping, concrete, instrumentation, electrical, insulation, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED HORIZONTAL TANK COST/ $ = (INSTALLED BASE COST) (FM) (Fp) (F,.) (F ) (f ~)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.94 - 2.10 percent of installed horizontal tank
cost and will depend upon corrosiveness of fluid, temperature, and pressure.
OPERATION COST
Horizontal tanks require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
91
-------
HU-1
HEATING UNIT
HEATING UNIT
1000000
o
a
g 100000
a
UJ
_i
_i
<
10000
0.1
1.0
CAPACITY (MM BTU/HOUR)
10.0
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
9
10
,000
,044
0.979
030
069
015
051
034
1-QS1
1.024
-------
HU-2
HEATING UNIT
Installed heating unit cost includes purchased cost of heating unit, accessories,
field erection by subcontractor, subcontractor's overhead and profit, piping,
concrete, instrumentation, electrical, insulation, paint, and indirect costs
(prime contractor engineering and construction overhead).
INSTALLED HEATING UNIT COST,$ = (INSTALLED BASE COST)(FD)
K
ANNUAL MAINTENANCE
Annual maintenance will vary from 2.6 - 2.9 percent of installed heating unit cost.
OPERATION COST
Heating units require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.083 12-18
Pulp and Paper 0.063 16
Mining 0.100 10
93
-------
1-1
INCINERATOR
INCINERATOR
1000000
I
CO
ce.
3
_i
o
a
CM
CT1
S 100000
o
co
S
10000
100
1000
CAPACITY (LBS/HOUR)
10000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
.000
,005
0.923
033
569
,043
,055
.082
056
1.014
94
-------
1-2
INCINERATOR
Installed incinerator cost includes purchased cost of incinerator, field erection,
piping, concrete, steel, instrumentation, insulation, paint, and indirect costs
(prime contractor engineering and construction overhead).
INSTALLED INCINERATOR COST.$ = (INSTALLED BASE COSl)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.4 percent of installed incinerator cost.
OPERATION COST
Incinerators require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
95
-------
IVS-1
IMPRESSED VOLTAGE SYSTEM
IMPRESSED VOLTAGE SYSTEM
100000
o
Q
O
U
LLJ
CO
<
oa
10000 -
1000
100
1000
CAPACITY (GALLONS)
10000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
R
1.000
1.062
0.986
0.992
1.326
0.966
1.273
1.073
1.219
1.082
96
-------
IVS-2
IMPRESSED VOLTAGE SYSTEM
Installed impressed voltage system cost includes purchased cost of tank, anodes,
rectifier, handling and setting, piping, concrete, steel, instrumentation,
electrical, paint, and indirect costs (prime contractor engineering and con-
struction overhead).
INSTALLED IMPRESSED VOLTAGE SYSTEM COST,$ = (INSTALLED BASE COST) (FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1 to 3 percent of installed impressed voltage
system cost.
OPERATION COST
Impressed voltage systems require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
97
-------
IE-1
' ION EXCHANGER
ION EXCHANGER
1000000
to
cr
o
Q
.CXI
en
100000
03
a
_l
<
10000
DESIGN ADJUSTMENT
Type
Anion
Hydrogen Cation
Sodium Cation
1.000
0.776
0.435
100
CAPACITY (CUBIC FEET)
1000
REGIONAL ADJUSTMENT
Region F
R
1.000
1.066
0.980
1.041
.083
.029
.073
.031
.074
1.034
98
-------
IE-2
ION EXCHANGER
Installed ion exchanger cost includes purchased cost of ion exchanger, auxiliaries,
ion exchange resin, handling and setting, piping, concrete, steel, instrumentation,
electrical, insulation, paint, and indirect costs (prime contractor engineering
and construction overhead).
INSTALLED ION EXCHANGER COST,$ = (INSTALLED BASE COST) (Fp)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3 percent of installed ion exchanger cost
and will depend upon cycle time, and fluid characteristics, packing, loading,
temperature and pressure.
OPERATION COST
Ion exchangers require between 0 and 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 . 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0-100 10-16
Mining 0.063-0.100 10-18
99
-------
K-l
KNEADER
KNEADER
1000000
I/I
ce
3
_i
o
Q
CS1
O1
o 100000
o
10000
10
100
CAPACITY (GALLONS)
1000
DESIGN ADJUSTMENT
Type
Stationary
Tilting
Vacuum Tilting
D
1.000
1.328
1.764
MATERIAL ADJUSTMENT
Material Fv
CS
SS304
SS316
Monel
0.000
0.402
0.625
0.802
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.034
0.942
1.033
1.113
1.035
1.048
1.058
.059
1.019
100
-------
K-2
KNEADER
Installed Kneade^cost includes purchased cost of kneader, motor and drive, accessories,
handling and setting, piping, concrete, instrumentation, electrical, paint, and indirect
costs (prime contractor engineering and construction overhead).
INSTALLED KNEADER COST.$ = (INSTALLED BASE COST)(FD +
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3 percent of installed kneader cost.
OPERATION COST
Kneaders require approximately 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.091 11
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.056-0.100 10-18
101
-------
LS-1
LAGOON SYSTEM
LAGOON SYSTEM
1000000
in
8 100000
10000
0.1
1.0
DESIGN FLOW (MGD>
10.0
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.427
0.913
.132
.416
.133
.353
.120
.060
1.179
102
-------
LS-2
LAGOON SYSTEM
Installed lagoon system cost includes excovation, aerators, piping, steel, electrical,
paint, and indirect costs (prime contractor engineering and construction overhead).
INSTALLED LAGOON SYSTEM COST,$ = (INSTALLED BASE COST)(FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3.89 percent of installed lagoon system.
OPERATION COST
Lagoon systems require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.040 25
Oil and Gas Refining 0.040 25
Resins and Polymers 0.040 25
Food and Beverage 0.040 25
Pulp and Paper 0.040 25
Mining 0.040 25
103
-------
MILL
DRIVER POWER (HP)
100
H-l
MILL
1000
1000000
o
Q
csi
r^,
01
o
u
Q
LU
_l
_l
<
100000
10000
10
100
CAPACITY (TONS/DAY)
1000
Type
DESIGN ADJUSTMENT
Curve F
D
Ball
Ball
Attrition
Swing Hammer
Mikro Pulverizer
Roller
Hammer
A
B
A
A
A
A
B
1.000
1.000
0.229
0.388
1.331
1.174
REGIONAL ADJUSTMENT
0.707
Region
1
2
3
4
5
6
7
9
10
1.000
1.021
0.935
1.028
1.126
1.035
1.046
1.056
I'.i
104
-------
M-2
HILL
Installed mill cost includes purchased cost of mill, accessories, motor and drive,
handling and setting, piping, concrete, instrumentation, electrical, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED MILL COST.$ = (INSTALLED BASE COST)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 6.1 - 6.5 percent of installed mill cost and will
depend upon material abrasiveness and process thruput.
OPERATION COST
Mills require between 0.25 and 0.50 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(Percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
IDS
-------
X-l
MIXER
DRIVER POWER (HP)
100
MIXER
1000
1000000
100000
19000
100
CAPACITY (CUBIC FEET)
DESIGN ADJUSTMENT
Curve
Type
Sigma
Fixed Propeller
Extruder
Muller Extruder
Spiral Ribbon
Two-Roll
Portable Propeller
Pan
1.000
1.000
1.000
0.694
1.000
0.660
0.185
2.372
REGIONAL ADJUSTMENT
Region Fr
1
2
3
4
5
6
7
8
9
10
000
037
941
034
129
034
047
057
063
1.021
106
-------
MX-2
MIXER
Installed mixer cost includes purchased cost of mixer, motor and drive, accessories,
handling and setting, piping, concrete, instrumentation, electrical, paint, and
indirect costs (prime contractor engineering and construction overhead).
INSTALLED MIXER COST.$ = (INSTALLED BASE COST) (Fp) (FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.33 - 1.36 percent of installed mixer cost.
OPERATION COST
Mixers require between 0.1 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage O.OS6-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
107
-------
p-1
PUMP
PUMP
100000
CAPACITY (GPM)
10
100
C/5
CtL
3
_i
o
a
CSJ
CT)
CO
o
CJ
cq
a
10000
1000
100
DESIGN ADJUSTMENT
Type Curve
Simplex
Duplex
Triplex
Diaphragm
Slurry
Rotary
Gear
D
000
298
960
000
104
0.466
0.590
REGIONAL ADJUSTMENT
Region Fp
1
2
3
4
5
6
7
8
9
10
000
064
978
034
076
027
066
029
067
1.033
108
-------
P-2
PUMP
Installed pump cost includes purchased cost of pump, motor and drive, base plate,
coupling, handling and setting, piping, concrete, instrumentation, electrical,
insulation, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED PUMP COST.$ = (INSTALLED BASE COST)(Fp) (FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from O.SS8 - 2.11 percent of installed pump cost and will
depend upon fluid velocity, temperature, pressure and fluid corrosive characteristics.
OPERATION COST
Pumps require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
109
-------
PKG-1
PACKAGING MACHINE
PACKAGING MACHINE
I
100K
CO
a:
3
_i
o
a
o
o
10K
100
BAGGING RATE (BAGS/MINUTE)
DESIGN ADJUSTMENT
Type FD
Bagging Machine 1.00
-Bagged by volume
Bagging Machine 3.23
-Bagged by weight
REGIONAL ADJUSTMENT
Region Fn
1
2
3
4
5
6
7
8
9
10
,000
.026
,938
.029
1.135
,035
,048
.058
058
1.016
110
-------
PKG-2
PACKAGING MACHINE
Installed packaging machine cost includes purchased cost of packaging machine,
accessories, motor and drive, handling and setting, piping and ductwork, concrete,
steel, instrumentation, electrical, insulation, paint, and indirect costs (prime
contractor engineering and construction overhead].
INSTALLED PACKAGING MACHINE COST,$ = (INSTALLED BASE COST)(Fn)(FD)
1J K
ANNUAL MAINTENANCE
Annual maintenance will vary from 2.4 - 2.6 percent of installed packaging machine
cost.
OPERATION COST
Packaging machines require between 0.5 and 1.0 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years]
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
111
-------
PR-1
PRESS
PRESS
1000000
o
Q
CNJ
r^.
en
100000
a
LLJ
_1
_1
<
10000
100
AREA (SQUARE FEET)
REGIONAL ADJUSTMENT
Region FR
1
2
3
4
5
6
7
8
9
10
1.000
0.988
0.896
.027
.185
.045
.048
.088
.039
1.005
1.0
100
1900
-------
PR-2
PRESS
Installed press cost includes purchased cost of press, setting and handling, piping,
concrete, instrumentation, electrical, paint, and indirect costs (prime contractor
engineering and construction overhead).
INSTALLED PRESS COST*$ a (INSTALLED BASE COST) (Fp)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 2.5 percent of installed press.
OPERATION COST
Presses require "between 0.125 and 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0,071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
113
-------
R-l
REACTOR
REACTOR
1000000
C/5
tYL
o
a
g 100000
<
co
10000
LOW PRESSURE FLUIDIZED
BED REACTOR
10
DIAMETER (FEET)
100
DESIGN ADJUSTMENT
Type F
D
One Stage
Two Stage
1.000
2.358
REGIONAL ADJUSTMENT
Region Fp
1
2
3
4
5
6
7
8
9
10
000
061
,984
,032
.073
.024
.062
.024
065
1.031
114
-------
R-2
REACTOR
Installed reactor cost includes purchased cost of reactor, auxiliaries, handling and
setting, piping, concrete, steel, instrumentation, electrical, insulation, paint,
and indirect costs (prime contractor engineering and construction overhead).
INSTALLED REACTOR COST,$ = (INSTALLED BASE COST)(Fn) (FD)
I) K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 2.47 percent of installed reactor cost.
OPERATION COST
Reactors require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical .050-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.056-0.100 10-18
115
-------
RD-1
ROTARY DRYER
ROTARY DRYER
1000000
CO
ce
3
_i
o
a
CNI
en
100000
10000
100
AREA (SQUARE FEET)
1000
DESIGN ADJUSTMENT
Type
Direct Gas Heating
Indirect Gas Heating
Vacuum
Jacketed Vacuum
1.000
1.380
4.192
5.870
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
R
1.000
1.059
0.957
1.045
1.123
,040
,074
.058
074
1.035
116
-------
RD-2
ROTARY DRYER
Installed rotary dryer cost includes purchased cost of rotary dryer, motor and drive,
accessories, handling and setting, piping, concrete, steel, instrumentation, electrical,
paint, and indirect costs (prime contractor engineering and construction overhead).
INSTALLED ROTARY DRYER COST,$ = (INSTALLED BASE COST) (Fn)(FD)
U K
ANNUAL MAINTENANCE
Annual maintenance will vary from 2.13 - 2.24 percent of installed dryer cost.
OPERATION COST
Rotary dryers require between 0.2 and 0.5 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
117
-------
ROS-1
REVERSE OSMOSIS SYSTEM
REVERSE OSMOSIS SYSTEM
10000
O
Q
CXI
rv,
en
1000
100
0.1
1.0
10.0
DESIGN ADJUSTMENT
CAPACITY (GPM)
Type
Hollow Fine Fiber
Spiral Wound
Tubular
D
1.000
1.390
1.615
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
000
07?
0.978
036
083
029
071
027
074
1.035
118
-------
ROS-2
REVERSE OSMOSIS SYSTEM
Installed reverse osmosis module cost includes purchased cost of reverse osmosis
module, membrane, membrane installation, handling and setting, piping, concrete,
instrumentation, paint, and indirect costs (prime contractor engineering and
construction overhead).
INSTALLED REVERSE OSMOSIS SYSTEM COST, $ = (INSTALLED BASE COST)(Fp)(FR)
ANNUAL MAINTENANCE
Annual maintenance will vary considerably depending upon application and membrane
life. Average annual maintenance can be estimated to be approximately 10 percent
of installed reverse osmosis module cost.
OPERATION COST
Reverse osmosis system require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
119
-------
RTC-1
RAILROAD TANK CAR
RAILROAD TANK CAR
100000
CO
ac.
o
o
o
u
10000
on
. 0°
Q
_1
<
1000
1000
10000
CAPACITY (GALLONS)
100000
120
-------
RTC-2
RAILROAD TANK CAR
Installed railroad tank car cost includes purchased cost of railroad rank car and
delivery.
INSTALLED RAILROAD TANK CAR COST,$ = INSTALLED BASE COST
ANNUAL MAINTENANCE
Annual maintenance will be approximately 4.9 percent of installed railroad tank car
cost.
OPERATION COST
Railroad tank cars require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE
(percent)
Heavy Chemical
Oil and Gas Refining
Resins and Polymers
Food and Beverage
Pulp and Paper
Mining
O.OSO-0.091
0.045
0.045
0.045
0.045
0.045
EXPECTED LIFETIME
(years)
11-20
22
22
22
22
22
121
-------
J-l
REFRIGERATION UNIT
REFRIGERATION UNIT
1000000
cc
3
_l
o
O
CM
01
CO
Q
100000
10000
100
DESIGN ADJUSTMENT
Type Temperature F
Mechanical 0UF
Steam Jet 60°F
D
1.000
0.836
CAPACITY (TONS)
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
9
10
.000
.067
0.973
,036
.091
.030
.061
.035
.067
1.031
TEMPERATURE ADJUSTMENT
(MECHANICAL ONLY)
-80 -60 -40 -20
20
40
60
80 100
TEMPERATURE
°F
122
-------
RU-2
REFRIGERATION UNIT
Installed refrigeration unit cost includes purchased cost of refrigeration unit,
auxiliaries, field erection and indirect costs (prime contractor engineering and
construction overhead).
INSTALLED REFRIGERATION UNIT COST,$ = (INSTALLED BASE COST) (FD)(FjMFR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 5 percent of installed refrigeration unit
cost.
OPERATION COST
Refrigeration units require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.0 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
123
-------
SCS-1
SUBMERGED COMBUSTION SYSTEM
SUBMERGED COMBUSTION SYSTEM
100000
10000
10
/
>
/
r
s
/
J
/
r—
-
00 10000 100000
CAPACITY (M BTU/HR)
REGIONAL ADJUSTMENT
Region F~
1
2
3
4
5
6
7
8
9
10
1.000
1.074
0.979
036
079
.027
1.071
026
,069
1.036
124
-------
SCS-2
SUBMERGED COMBUSTION SYSTEM
Installed submerged combustion system cost includes purchased cost of evaporator,
blower, drives, heating unit, handling and setting, piping, concrete, steel,
instrumentation, electrical, insulation, paint, and indirect costs (prime contractor
engineering and construction overhead).
INSTALLED SUBMERGED COMBUSTION SYSTEM COST,$ = (INSTALLED BASE COST)(FD)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.2 to 6 percent of installed submerged combustion
system cost.
OPERATION COST
Submerged combustion systems require between 0.125 and 1.0 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.091 11
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056-0.083 12-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
125
-------
SS-1
SEDIMENTATION SYSTEM
SEDIMENTATION SYSTEM
1000000
o
o
CN
r-^
en
CO
o
100000
i*
CO
10000
1.0
10.0
100.0
CAPACITY (MGD)
REGIONAL ADJUSTMENT
Region FR
1
2
3
4
5
6
7
8
9
10
000
045
0.947
1.043
1.133
041
066
065
067
1.029
126
-------
SS-2
SEDIMENTATION SYSTEM
Installed sedimentation system cost includes purchased cost of tanks, pumps, notors
and drives, piping, concrete, structural steel, instrumentation, electrical, paint,
and indirect costs (prime contractor engineering and construction overhead).
INSTALLED SEDIMENTATION SYSTEM COST, $ = (INSTALLED BASE COST) (FJ
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 5-16 percent of installed sedimentation
system cost.
OPERATION COST
Sedimentation systems require no operator attention.
PROBABLE DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.016-0.040 25-60
Oil and Gas Refining 0.016-0.040 25-60
Resins and Polymers 0.016-0.040 25-60
Food and Beverage 0.016-0.040 25-60
Pulp and Paper 0.016-0.040 25-60
Mining 0.016-0.040 25-60
127
-------
STK-1
STACK
STACK
100000
o
a
CNl
t\
CD
to
O
10000
1000
10
100
HEIGHT (FEET)
1000
DESIGN ADJUSTMENT
Diameter F
(inches)
D
24
36
48
1.000
2.220
2.970
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
000
061
0.984
032
073
024
062
024
065
1.031
128
-------
STK-2
STACK
Installed stack cost includes purchased cost of stack, handling and setting, piping
and duckwork, concrete, steel, insulation, paint, and indirect costs (prime
contractor engineering and construction overhead).
INSTALLED STACK COST,$ = (INSTALLED BASE COST) (Fn)(F0)
v K
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.2 to 1 percent of installed stack cost.
OPERATION COST
Stacks require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
129
-------
T-l
THICKENER
THICKENER
1000000
o
Q
csi
r-^
en
100000
10000
100
DIAMETER (FEET)
1000
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
R
.000
.061
.984
1.032
0/3
024
062
024
065
1.031
130
-------
T-2
THICKENER
Installed thickener cost includes purchased cost of thickener, erection, site
preparation, pumps, piping, concrete, steel, instrumentation, electrical,
paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED THICKENER COST,$ = (INSTALLED BASE COST)(FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1 percent of installed thickener cost.
OPERATION COST
Thickeners require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.016-0.040 25-60
Oil and Gas Refining 0.016-0.040 25-60
Resins and Polymers 0.016-0.040 25-60
Food and Beverage 0.016-0.040 25-60
Pulp and Paper 0.016-0.040 25-60
Mining 0.016-0.040 25-60
131
-------
TF-1
TRICKLING FILTER
TRICKLING FILTER
10000000
100000
100
1000
CAPACITY (GPM)
10000
REGIONAL ADJUSTMENT
Eegion
1
2
3
4
5
6
7
8
9
10
R
1.000
1.045
0.947
043
133
041
066
065
067
1.029
132
-------
TF-2
TRICKLING FILTER
Installed trickling filter cost includes purchased cost of mechanism, notor and drive,
rock packing, setting packing, concrete, steel, instrumentation, electrical, insulation,
paint and indirect costs (prime contractor engineering and construction overhead).
INSTALLED TRICKLING FILTER COST,$ - (INSTALLED BASE COST) (FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3.3 percent of the installed trickling filter
cost.
OPERATION COST
Trickling filters require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.025-0.050 20-40
Oil and Gas Refining 0.025-0.050 20-40
Resins and Polymers 0.025-0.050 20-40
Food and Beverage 0.025-0.050 20-40
Pulp and Paper 0.025-0.050 20-40
Municipal Usage 0.025-0.050 20-40
133
-------
TW-1
TRAY TOWER
TOWER
1000000
_
o
Q
CN1
fv
en
<
ea
100000
10000
DESIGN ADJUSTMENT
Type
Bubble Cap
Koch Kascade
Plate Tray
Sieve Tray
Turbo Grid
Valve Tray
D
1.000
1.243
0.852
0.874
0.855
0.911
MATERIAL ADJUSTMENT
Material F
M
CS
SS304
SS316
SS347
Ni
Cu
Brass
A 515 CS
Monel
Moly
Ti
000
300
503
578
579
6.056
5.102
0.991
2.419
4.193
100
DIAMETER (INCHES)
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
1.000
1.062
0.977
1.035
1.080
1.026
1.064
1.028
1.071
1.028
1000
5.052
500 1000
PRESSURE
1500
1800
134
TEMPERATURE ADJUSTMENT
1.00
500 1000
TEMPERATURE (°p)
1500
-------
TW-2
TRAY TOWER
Installed tray tower cost includes purchased cost of tray tower, trays, handling and
setting, piping, concrete, steel, instrumentation, electrical, paint, and indirect
costs (prime contractor engineering and construction overhead).
INSTALLED TRAY TOWER COST,$ = (INSTALLED BASE COST") (Fp) (FD) (FM) (FR) (F-,.)
ANNUAL MAINTENANCE
Annual maintenance will vary from 7.35 - 10.71 percent of installed tray tower cost
and will depend upon temperature, pressure, fluid corrosivity and fluid velocity.
OPERATION COST
Tray towers require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056- .083 12-18
Pulp and Paper 0.063 16
Mining 0.063-0.100 10-18
135
-------
TW-3
COOLING TOWERS
COOLING TOWERS
1000000
C
100000 -
10000
1000
10000
CAPACITY (GPM)
100000
REGIONAL ADJUSTMENT
Region F
1
2
3
4
5
6
7
8
9
10
000
061
0.984
1.052
1.073
024
062
024
065
1.031
136
-------
TVH
COOLING TOWERS
Installed cooling tower cost includes purchased cost of cooling tower, basin,
handling and setting, piping, concrete foundations and footings, instrumentation,
paint, and indirect costs (prime contractor engineering and construction overhead],
INSTALLED COOLING TOWER COST, $ = (INSTALLED BASE COST) (FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3 percent of installed cooling tower cost.
OPERATION COST
Cooling towers require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056- .083 12-18
Pulp and Paper 0.063 16
Mining 0.063-0.100 10-18
137
-------
TW-5
PACKED COLUMN
PACKED COLUMN
1000000
CNI
"-»
CT1
100000
10000
100
DIAMETER (INCHES)
1000
MATERIAL ADJUSTMENT
Material F.
CS
SS304
SS347
Ni
Ti
Cu
Al
A 515 CS
A 204 CS
M
1.000
1.042
1.060
1.801
2.420
3.365
3.339
1.007
1.064
REGIONAL ADJUSTMENT
Region Fn
1
2
3
4
5
6
7
8
9
10
000
.076
,073
,043
,097
.034
.042
.036
079
1.037
4-° \— PRESSURE ADJUSTMENT
500
1000
1500 180
138
1.12
1.08
1.00
- TEMPERATURE ADJUSTMENT
500 1000
TEMPERATURE (°F)
1500
-------
PACKING TYPE
TW-6
PACKED COLUMN
Activated carbon
Alumina
Calcium chloride
Coke
Crushed limestone
Resin
Silica gel
0.5 inch diameter berl saddles, stoneware
.75 inch diameter berl saddles, stoneware
1.0 inch diameter berl saddles, stoneware
1.5 inch diameter berl saddles, stoneware
0.5 inch diameter berl saddles, porcelain
.75 inch diameter berl saddles, porcelain
1.0 inch diameter berl saddles, porcelain
1.5 inch diameter berl saddles, porcelain
0.5 inch diameter berl saddles, steel
.75 inch diameter berl saddles, steel
1.0 inch diameter berl saddles, steel
1.5 inch diameter berl saddles, steel
0.5 inch diameter berl saddles, stainless steel
.75 inch diameter berl saddles, stainless steel
1.0 inch diameter berl saddles, stainless steel
1.5 inch diameter berl saddles,
0.5 inch diameter berl saddles,
stainless steel
karbate
.75 inch diameter berl saddles, karbate
1.0 inch diameter berl saddles, karbate
1.5 inch diameter berl saddles, karbate
0.5 inch diameter intalox saddles, ceramic
1.0 inch diameter intalox saddles, ceramic
1.5 inch diameter intalox saddles, ceramic
2.0 inch diameter intalox saddles, ceramic
1.0 inch diameter pall rings, ceramic
0.5 inch diameter pall rings, polypropylene
1.0 inch diameter pall rings, polypropylene
1.5 inch diameter pall rings, polypropylene
2.0 inch diameter pall rings, polypropylene
0.5 inch diameter pall rings, stainless steel
1.0 inch diameter pall rings, stainless steel
1.5 inch diameter pall rings, stainless steel
2.0 inch diameter pall rings, stainless steel
1
1
1
1
2
3
1
1
2
3
1
1
2
3
1
1
2
3
1
1
2
3
.0
.5
.0
.5
.0
.0
.0
.5
.0
.0
.0
.5
.0
.0
.0
.5
.0
.0
.0
.5
.0
.0
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
inch
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
diameter
Tellerettes H.D.
Tellerettes L.D.
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rashig
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings,
rings ,
polyethylene 1
polyethylene 1
carbon
carbon
stoneware
stoneware
stoneware
stoneware
porcelain
porcelain
porcelain
porcelain
stainless
stainless
stainless
stainless
karbate
karbate
karbate
karbate
steel
steel
steel
steel
inch
inch
steel
steel
steel
steel
16.40
15.10
4.11
2.05
4.11
93.10
34.20
32.80
21.90
13.10
9.85
39.40
26.30
15.80
11.80
65.70
43.80
26.30
19.70
82.10
54.70
32.80
24.60
328.00
219.00
131.00
98.50
33.40
13.30
10.20
10.40
71.00
58.20
36.90
29.50
26.30
26.50
13.60
11.80
9.80
26.40
26.10
6.30
5.06
4.38
3.70
7.56
6.08
5.26
4.43
15.70
12.70
10.90
9.24
63.00
50.60
43.80
37.00
12.60
10.10
8.76
7.39
26.30
22.70
139
-------
TW-7
PACKED COLUMN
Installed packed column cost includes purchased cost of packed column less packing
and packing installation, handling and setting, piping, concrete, steel, instrumenta-
tion, electrical, insulation, paint, and indirect costs (prime contractor engineering
and construction overhead).
/PACKINGS
INSTALLED PACKED COLUMN COST,$ => (INSTALLED BASE COST) (FM) (Fp) (FJ (F-,.) + (FK) ( ^LUME ]
\ CUBIC /
VFEET J
ANNUAL MAINTENANCE
Annual maintenance will vary from 3.60 - 3.97 percent of installed packed column cost
and will depend upon fluid corrosivity, temperature, pressure, and fluid velocity.
OPERATION COST
Packed columns require approximately 0.25 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071 14
Food and Beverage 0.056- .083 12-18
Pulp and Paper 0.063 16
Mining 0.063-0.100 10-18
140
-------
US-1
ULTRAFILTRATION SYSTEM
ULTRAFILTRATION SYSTEM
10000
o
a
O
O
s
a
UJ
i*
to
1000
1.0
CAPACITY (GPM)
10.0
REGIONAL ADJUSTMENT
Region Fp
1.000
1.064
0.978
034
076
027
066
029
067
1.033
141
-------
US-2
ULTRAFILTRATION SYSTEM
Installed ultrafiltration system cost includes purchased cost of membrane modules,
membranes, pressurization pump, recirculation pump, handling and setting, piping,
concrete, steel, instrumentation, electrical, paint, and indirect costs (prime
contractor engineering and construction overhead) .
INSTALLED ULTRAFILTRATION SYSTEM COST,$ = (INSTALLED BASE COST)(FD)
K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1 to 3 percent of installed ultrafiltration
system cost.
OPERATION COST
Ultrafiltration systems require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.04S 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
142
-------
VP-1
VACUUM PUMP
VACUUM PUMP
100000
CNJ
l\
en
10000
1000
10
100
CAPACITY (CFM)
1000
REGIONAL ADJUSTMENT
Region F
9
10
R
1.000
1.073
0.979
1.038
1.084
025
062
039
069
1.031
143
-------
VP-2
VACUUM PUMP
Installed vacuum pump cost includes purchased cost of vacuum pump, motor and drive,
handling and setting, piping, concrete, instrumentation, electrical, insulation, paint,
and indirect costs (prime contractor engineering and construction overhead].
INSTALLED VACUUM PUMP COST-S = (INSTALLED BASE COST)(FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 0.75 percent of the installed vacuum pump
cost.
OPERATION COST
Vacuum pumps require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
0.063-0.100 10-18
144
-------
VS-1
VIBRATING SCREEN
VIBRATING SCREEN
100000 r—
10000
1000
100
AREA (SQUARE FEET)
DESIGN ADJUSTMENT
Type F
D
Single Deck
Two Deck
Three Deck
1.000
1.192
1.436
REGIONAL ADJUSTMENT
Region Fn
1
2
3
4
5
6
7
8
9
10
1.000
0.996
0.897
034
193
049
047
098
1.057
1.009
145
-------
VS-2
VIBRATING SCREEN
Installed vibrating screen cost includes purchased cost of vibrating screen motor
and drive, handling and setting, piping and ductwork, concrete, instrumentation,
electrical, paint, and indirect costs (prime contractor engineering and construction
overhead).
INSTALLED VIBRATING SCREEN COST,$ = (INSTALLED BASE COST)(Fn)(FD)
U K
ANNUAL MAINTENANCE
Annual maintenance will be approximately 1.87 percent of installed vibrating screen cost
and will depend upon material corrosivity and abrasiveness.
OPERATION COST
Vibrating screens require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.05-0.091 11-20
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.091 11-18
Pulp and Paper 0.063-0.100 10-16
Mining 0.063-0.100 10-18
146
-------
VT-1
VERTICAL TANK
VERTICAL TANK
10000
100000
CAPACITY (GALLONS)
100000
cc
f
_!
O
Q
O-J
1500
147
-------
VI-2
VERTICAL TANK
Installed vertical tank cost includes purchased cost of vertical tank (field
erection for large size vessels), handling and setting, piping, concrete,
instrumentation, insulation, paint, and indirect costs (prime contractor
engineering and construction overhead).
INSTALLED VERTICAL TANK COST,$ = (INSTALLED BASE COST) (Fn) (FM) (FJ (FD) (F )
U Pi r K \
ANNUAL MAINTENANCE
Annual maintenance will vary from 1.93 - 2.61 percent of installed vertical tank cost
and will depend upon temperature, pressure, fluid corrosivity and cycle time.
OPERATION COST
Vertical tanks require no operator attention.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.04S 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
148
-------
WTS-1
WATER TREATMENT SYSTEM
WATER TREATMENT SYSTEM
1000000
<
_1
_1
o
CN
01
CO
o
100000
o
UJ
10000
100
10
10*
1000
CAPACITY (GPM)
10000
Type
DESIGN ADJUSTMENT
Curve
REGIONAL ADJUSTMENT
Region FR
Demineralizing System
Softening System
Filtering System
Pumping Station
Cooling System
Outfall System
(10000 ft)
00
000
000
000
000
1.000
1
2
3
4
5
6
7
8
9
10
1.000
1.045
0.947
043
133
,041
066
.065
,067
1.029
149
-------
WTS-2
WATER TREATMENT SYSTEM
Installed water treatment system cost includes purchased cost of water treatment
system, pumps, drives, necessary closed pump station buildings (if required),
handling and setting, piping, concrete, basins, pits and foundations, steel,
instrumentation, electrical, paint, and indirect costs (prime contractor engineering
and construction overhead).
INSTALLED WATER TREATMENT SYSTEM COST/ $ = (INSTALLED BASE COST) (FD) (FR)
ANNUAL MAINTENANCE
Annual maintenance will vary from 0.1 to 8 percent of installed water treatment
system cost and will primarily depend upon influent water quality, flowrate, and
cycling.
OPERATION COST
Water treatment systems require between 0.125 and 1.0 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.016-0.040 25-60
Oil and Gas Refining 0.016-0.040 25-60
Resins and Polymers 0.016-0.040 25-60
Food and Beverage 0.016-0.040 25-60
Pulp and Paper 0.016-0.040 25-60
Mining 0.016-0.040 25-60
150
-------
WTS-3
STEAM BOILER
STEAM BOILER
1000000
U)
OL
o
Q
CSI
r-^
en
to
o
05
g
100000
10000
10000
100000
CAPACITY (IBS STEAM/HR)
1000000
REGIONAL ADJUSTMENT
Region F^
—I— i.ooo
2 1.044
3 0.979
4 1.030
5 1.069
6 1.015
7 1.051
8 1.034
9 1.051
10 1.024
151
-------
WTS-4
STEAM BOILER
Installed steam boiler cost includes purchased cost of boiler, forced draft fans,
burners, soot blowers, boiler feedwater pumps, feed water deaerator, chemical
injection system, stock, handling and setting, piping, concrete, steel,
instrumentation, electrical, insulation, paint, and indirect costs (prime
contractor engineering and construction overhead).
INSTALLED STEAM BOILER COST, $ = (INSTALLED BASE COSTMF,,) (FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3 percent of installed steam boiler cost.
OPERATION COST
Steam boilers require between 0.125 and 1.0 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.071-0.091 11-14
Oil and Gas Refining 0.063-0.071 14-16
Resins and Polymers 0.071-0.111 9-14
Food and Beverage 0.056-0.083 12-18
Pulp and Paper 0.063 16
Mining 0.100 10
152
-------
WATER STILL
WTS-5
WATER STILL
100000
cc
3
_1
o
Q
CM
cn
<
CQ
a
LU
10000
1000
10
CAPACITY (GALLONS/DAY)
100
REGIONAL ADJUSTMENT
Region
1
2
3
4
5
6
7
8
9
10
000
044
0.979
,030
069
015
,051
034
051
1.024
153
-------
WTS-6
WATER STILL
Installed water still cost includes purchased cost of still, handling and setting,
piping, concrete, steel, instrumentation, insulation, paint, and indirect costs
(prime contractor engineering and construction overhead).
INSTALLED WATER STILL COST,$ = (INSTALLED BASE COST) (FR)
ANNUAL MAINTENANCE
Annual maintenance will be approximately 3 percent of installed water still cost.
OPERATION COST
Water stills require between 0.05 and 0.2 operators per shift.
PROBABLE ANNUAL DEPRECIATION RATE
INDUSTRY GROUP DEPRECIATION RATE EXPECTED LIFETIME
(percent) (years)
Heavy Chemical 0.050-0.091 11-20
Oil and Gas Refining 0.045 22
Resins and Polymers 0.045 22
Food and Beverage 0.045 22
Pulp and Paper 0.045 22
Mining 0.045 22
154
-------
SECTION IV
ACKNOWLEDGEMENTS
This project was directed by Mr. Herbert G. Blecker. Assistance in this effort
by many individuals in and out of government has been extremely helpful. We
especially acknowledge those vendors and contractors who have assisted in the
effort. We are grateful for the guidance provided by Mr. Paul Greenberger and
other members of the Environmental Protection Agency Staff.
155
-------
SECTION V
REFERENCES
1. Blecker, H. G. and Nichols, T. M. , C0gT® System User's Manual, Second Edition,
ICARUS Corporation, Silver Spring, Maryland, January 1973.
2. Blecker, H. G., From Process Flowsheet to Detailed Estimate, presented at the
American Institute of Chemical Engineers 18th Annual All-Day Meeting, University
of Delaware, March 27, 1973.
3. Blecker, H. G., Computer Simulation of Definitive Estimates, to be presented at
the National Meeting of the American Association of Cost Engineers, St. Louis,
Mo. , June 1973.
4. Blecker, H. G., Cost Models: A Computerized Approach to the Simulation of
Equipment Cost, 1972 Transactions of the American Association of Cost Engineers.
5. Blecker, H. G., Simulation of Chemical Processing Plant Investment by Computer,
1972 Transactions of the Summer Computer Simulation Conference, San Diego,
California, June 14-16, 1972.
6. U.S. Department of Commerce, Selected Climatic Maps of the United States, U.S.
Government Printing Office, Washington, D.C., 1966.
7. Foster, N., 1972 Dodge Construction and Scheduling Manual, McGraw-Hill Information
Systems Company, New York, N.Y., 1972.
8. McKee-Berger-Mansueto Inc., Building Cost File, Construction Publishing Company,
Inc., New York, N.Y., 1973.
9. Rase, H. F., and Barrow, M.H..Project Engineering of Process Plants, John Wiley
and Sons, Inc., New York, N.Y. , May 19677
10. Ludwig, E. E., Applied Process Design for Chemical and Petrochemical Plants, Vol.
I-III, Gulf Publishing Company, Houston, Texas, 1964.
156
-------
SECTION VI
GLOSSARY
Adjustment Factor - An additive or multiplicative factor for adjusting installed base
cost to obtain installed cost. The adjustments may be regional (for location of
installation), design (for the type of design), pressure, temperature, cost escalation,
or other pertinent parameters.
Cost Escalation Factor - See Adjustment Factor, a composite of the Marshall fj Stevens
Index and the Engineering News Record Construction Cost Index.
Design Adjustment Factor - See Adjustment Factor.
Equipment Item - A piece of processing equipment. Generally refers to the piece as
purchased and before installation.
Installed Base Cost - The installed cost for an equipment module in a nominal location
with nominal design and operating characteristics.
Installed Cost - The cost including purchased equipment, material and labor requirements
forinstallation, contractors engineering and overhead. For processes, includes
contractors fee, contingencies, and land cost as well.
Installed Equipment Module - An equipment item together with its usual accessories, all
completely installed.
Key Cost Parameter - The single physical or capacity characteristic of an installed
equipment module which is most directly related to installed cost.
Labor to Material Ratio - The ratio of labor to material requirements in installed
equipment module.
Pressure Adjustment Factor - See Adjustment Factor.
Regional Adjustment Factor - See Adjustment Factor.
Subcontract Cost - The fee paid to another by the contractor for services, such as
erecting a building, completing yard improvements, etc.
Temperature Adjustment Factor - See Adjustment Factor.
Additional glossaries may be found in
1. Industrial $ Engineering Chemi.stry 52 (6), 69 (1960).
2. Industrial § Engineering Chemistry S2_ (7), S3 ( 960).
3. J. H. Perry, Chemical Engineers' Handbook, 4th Ed., pages 26-2, to 26-5.
157
-------
SECTION VII
APPENDICES
Page
A. Cost Modules 159
B. Regional Data 165
C. Frost Depth I66
D. Isotach 167
E. Selected Material Costs 168
F. Cross Reference Index 169
G. Data Sheet Index I83
158
-------
APPENDIX A
COST MODULES
EQUIPMENT COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
INPUT
FROM
USER
INPUT
TRANSLATOR
EQUIPMENT EXECUTIVE
'
j
r
STORAGE
Cost Symbols
Equipment Types
Equipment Costs
Unit Man hours
C
aft Mix
Labor Rales
Equ
pment Rental
i
i
'
ALGORITHMS
Equipment Design
Sizing Techniques
Field Labor Manhours
Construction Equip me
Modola
t Relationships
Material Component
All equipment necessary for the processing plant
as indicated on flowsheets, equipment lists, etc
Labor Component
All labor operations necessary to unload, store, set in
site Includes labor to assemble, erect and dismantle
rigging poles and guy derricks when necessary
PIPING COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
1
' i
INPUT
TRANSLATOR
INPUT
FROM
USER
PIPING EXECUTIVE
STORAGE
Con Symboli
Mat.ml Unit Com
Unit Mmhoin
Crlft Mil
Libor RitK
Eqiiipmint flmul
ALGORITHMS
Sizing Routine*
Lint Specifications
Material Quantities
Field Labor Minhoun
Construction Equipment
Modular Relationships
OUTPUT
' TO USER
Ma tentl Cotr-.pomnt
• Shop fabricated materiel - process, auxiliary, utility
• Field fabricated material - process, auxiliary, utility
e Fi« d MMmlily material (valvn, flengei, expansion joint*,
etc )
e Smalt piping under 2" (screwed, socket in weld, steam
tracing, tubing, velvet, etc I
* Underground piping (cast iron, vitrified clay, concrete
tnnsita, tic }
e Sp«i«l ftbr.cattd lyttemi (rubber Imtd. gfeu lined, etc ,
as rftguired by • perticulcr proceu)
• Shoes, gutdct, brackiti, climpi, hangen, insulation
wppom, etc.
e Scaffoldings required
Ltbor Component
• Unload itore, handle
• F.eJd fabrication (tit labor opwauon* performed in the
jobsite weld shop uch ai cutting/bevelmg, preheating,
welding, x-ray, strew relief, etc )
• Pipe erection (all labor operations to erect shop fabricated
and field fabricated spools in piece, install pipe, vatvei,
and other assembly material, coat and wrap underground
piping, stress relief and x r»y field weldf, etc (
• Small piping under 2" (all labor operations to install
screwed, locket weld, steam tracing, tubing, etc )
• Special fabricated systems (aH labor operation*
to inttall rubber l>r>ed, glist lined and other spec*)
prefabricated components)
• Labor manhours to install shoes, hangen, guidw,
brackets, etc , necessary to support piping systems
• Scaf'olding labor as required
159
-------
CONCRETE COST ELEMENT
CONCRETE EXECUTIVE
1 '
STORAGE
Cost Symbols
Foundation Types
Structural Types
Material Unit Costs
Unit Manhours
Craft Mix
Labor Rate
s
Equipment Rental
i
<
i
ALGORITHMS
Design Routines
Material Quantities
Field Labor Manhours
Construction Equipmen
Modular Relationships
Material Component
• Concrete (redi mix, cement, sdnd, aggregate add misc ,
color, testing, etc )
• Forming (plywood, sonotube, metal forms, backup
lumber, nails, clamps, etc 1
• Reinforcing (rebar, tie wire, mesh, etc )
• Accessories (anchor bolts, curb angles, fireproofmg
material, hardware, etc)
• Concrete pipe supports and sleepers
» Miscellaneous ttiench covers, basin covers, manholes,
catch basins, manholes, etc )
• Weather protection (shelters, heating equipment,
covers, etc )
• Scaffolding as required
Labor Component
• Unload, store, handle
• Equipment foundations (all labor operations necessary
to install rebar. forming and mass pour concrete)
• Pipe supports (all labor operations to install precast
supports, sleepers, poured m place items, etc }
• Basins, manholes, trenches (all labor operations to install
cooling towet basins, manholes, catch basins, pull boxes,
valve boxes, trenches, etc )
• Concrete paving (all labor operations necessary to install
paving, roads, gutters, envelopes, etc )
• Miscellaneous (all labor required to grout and finish
equipment setting, apply special coatings to foundation
slabs, basins, etc )
• Scaffolding labor as required
STRUCTURAL STEEL COST ELEMENT
INPUT ,WUT
FROM rngM
SYSTEM usfj1
EXECUTIVE ' ' "
INPUT
TRANSLATOR
*
1 STRUCTURAL STEEL EXECUTIVE 1
1 1
STORAGE
Cost Symbols
Structural Types
Material Unit Costs
Unit Mart hours
Craft Mix
Labor Rates
Equipment Rental
1 •
ALGORITHMS
Design Routines
MatenaJ Quantities
Field Labor Manhoun
Construction Equipment
Modular Relationships
r
TD\»BSTEM •« 1 OUTPUT 1 b- OUTi>llT
EXECUTIVE 1 GENERATOR | " TO USER
Material Component
• Steel structures (for process equipment access and sup-
port, including ladders, platform walkways, guard rails,
crane rails, all appertenances, etc )
• Ladders, platforms, and walkways (when not attached
to vessels, boilers, and coolers, etc J
* Steel pipe supports and sleepers
• Scaffolding as required
Labor Component
# Un oad, store, handle
• Steel structures (all labor operations to erect steel
structures on the jobsite)
• Ladders and platforms (all labor operations to erect
on the jobsite)
* Steel pipe supports (all labor to assemble, erect or
install on the jobs te)
• Scaffold ng labor as required
160
-------
INSTRUMENTATION COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
INPUT
TRANSLATOR
-INPUT
FROM
USER
INSTRUMENTATION EXECUTIVE
1
i
STORAGE
Cost Symbols
Instrur
rent Uni
Costs
Material Unit Costs
Unit Ma n hours
Craft Mix
Labor Rates
t
i
t
ALGORITHMS
Mater
Field
a! Quantities
abor Ma
n hours
Modular Relationships
FEEDBACK
TQ SYSTEM -
EXECUTIVE
OUTPUT
GENERATOR
. OUTPUT
TO USER
Mater/31 Component
• Major offline items (analyzers, etc )
• Sensing devices (temperature, pressure, flow, gauge
glasses, level indicators, etc }
• Control devices (control valves, power operators, etc )
• Miscellaneous (relief valves, steam traps, switches,
alarms, s
• Field assert
racks, etc )
• Co']*iot panels and pam
• Scaffolding as required
ids, etc )
ibly material (piping, tubing, supports, tube
Labor Component
• Unload, store, handle
• Major offline items (all labor operatic
nstall ,
, etc )
ary to
ients (all labor operations necessary to
its in the field)
• Loca
install sensing and control u
• Miscellaneous (all labor operations necessary to install
relief valves, steam traps, switches, alarms, solenoids,
etc)
• Field assembly (all labor operations to install main
control tubing runs, etc I
• Check out, calibrate, and test
• Scaffolding labor as required
ELECTRICAL COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
1
' i
INPUT
TRANSLATOR
INPUT
FROM
USER
ELECTRICAL EXECUTIVE
\
> t
STORAGE
Cost Symbols
Un
U.i
t Costs
t Man hours
Craft Mix
Labor Rates
1
v
L
ALGORITHMS
Material Quantities
Labor Manhou
S
Field Labor Ma nhours
Modular Relationship
ion and control (sub stations, switchgear
starters, bus ducts, etc )
street lights, etc)
t Grounding and Cathodic Protectio
recorder
interlock systems, etc )
speakers, fire reporting systems, etc )
> Pole lines (pole mounted instdllation for power distribu
tion, etc )
i Scaffolding as required
Labor Component
• Unload, store, handle
• Power distribution and control [All labor operations
necessary to install major items of electrical equipment
This includes handling, storing, setting in place and testir
conduit and accessories for power feeders and motor runs
both above and below ground level)
wire and cable for power feeders and motor runs both
above and below ground level, instrumentation, communi
cations, etc ) Test and check out
Pole lines (all labor operations necessary to install wood
poles set and dress, install conductors, etc 1 Test and
check out
161
-------
INSULATION COST ELEMENT
INSULATION EXECUTIVE
i
r
STORAGE
Cost Symbols
U
it Costs
Unit Man hours
Craft Mix
Labor Rates
i
i
t
ALGORITHMS
Material Quantities
Field
Modu
.abor Ma
nhours
ar Relationships
FEEDBACK
TO SYSTEM
EXECUTIVE
H OUTPUT ^
GENERATOR I
OUTPUT
TO USER
Material Component
• Equipment insulation material {special molding, covers,
flat sheets, etc )
covers, flange covers, etc
• Tiewtre, mesh, etc
• Scaffolding as required
> Unload, store and handle
items and piping as required
t ScaHolding labor as required
PAINT COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
INPUT
FROM
USER
INPUT
TRANSLATOR
T
PAINT EXECUTIVE
'
i
STORAGE
Cost Symbols
Un
t Costs
Unit Manhours
Cra
ft Mix
Labor Rates
i
i
ALGORITHMS
Material Quantities
Field
Modu
.abor Ma
nhour
ar Relationships
Material Component
• Paint material special coatings, etc
• Sandblasting material as required
• Scaffolding as required
Labor Component
• Unload, store, and handle
• Labor to apply paint (spray, brush, etc )
• Scaffolding labor as required
162
-------
PLANT BUILDING COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
1
' i
r
INPUT
TRANSLATOR
INPUT
FROM
USER
PLANT BUILDING EXECUTIVE
1
i
STORAGE
Type Symbols
foundat ons
Shell
,
3oof
Unit Costs
i
>
ALGORITHMS
Building Costs
Service Costs
Modular Relationships
FEEDBACK
TO SYSTEM
EXECUTIVE
OUTPUT -
GENERATOR
. OUTPUT
TO USER
Material Component
required (administration workshops, control
rooms, steel structures, etc )
Labor Component
All labor necessary to construct buildings as
required (plus burden and overhead if buildings
subcontracted)
ENGINEERING COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
INPUT
- FROM
USER
INPUT
TRANSLATOR
ENGINEERING EXECUTIVE
1
/
STORAGE
Unit Manhours
Unit Rates
n direct Relationships
i
i
ALGORITHMS
Direct Labor Manhours
ndirect Costi
Mod u la
r Relationships
indirect cosls
• Payroll burdens
• Office expense
•Office overhead
Labor Component
All home office labor for the following engineering
act (vi ties
• Project
• Process
• Design
• Procurement
• Home Office Construction
163
-------
SITE WORK COST ELEMENT
INPUT
FROM
SYSTEM
EXECUTIVE
1
r i
INPUT
TRANSLATOR
USER
INPUT
DATA
SITE WORK EXECUTIVE
STORAGE
Work Items
Unit Costs
FEEDBACK
TO SYSTEM
EXECUTIVE
ALGORITHMS
Work Item Quantities
—I
OUTPUT
GENERATOR
OUTPUT
TO USER
Material Component
All material and equipment necessary for site work
• Roads, walkways, paving
• Site clearing, excavation and grading
• Sewers and underground
• Landscaping, etc.
Labor Component
Alt labor necessary for site work
• Roads, walkways, paving
• Site clearing, excavation and grading
• Sewers and underground
• Landscaping, etc.
CONSTRUCTION OVERHEAD COST ELEMENT
FROM
SYSTEM
EXECUTIVE
<
' 1
INPUT
TRANSLATOR
FROM
USER
CONSTRUCTION OVERHEAD EXECUTIVE
Cost Relationships
Unit Manhours
Unit Rates
Labor Rates
Craft Benefits
Payroll Burdens
Equipment Rental Rates
Temporary Construction Facilities
Construction Services
Field Supervision
Payroll Burdens and Insurants
Construction Equipment
Small Tools
Modular Relationships
FEEDBACK
TO SYSTEM
EXECUTIVE
OUTPUT
GENERATOR
OUTPUT
TO USER
Material Component
• AM material necessary to
• Payroll burdens and expe
field labor and supervisio
• Construction equipment
construct temporary facilities
nse on direct and indirect
n
rental and small tool cost
Labor Component
• All labor necessary to construct temporary facilities
and provide construction services in the field
• All field staff labor and costs
164
-------
APPENDIX B
REGIONAL DATA
AVERAGE
i
REGION
1
2
3
4
5
6
7
8
9
10
WIND
SPEED
RANGE
(MPH)
67-100
67-100
67-90
67-120
67-100
67-100
67-100
75-100
60-90
60-95
FROST
LINE
RANGE
(INCHES)
25-60
.15-45
10-25
0-10
10-60
0-15
10-45
5-60
0-10
0-25
SOIL SOIL
TYPE LOADING
(LBS/FT3)
DRY SAND
SAND
DRY SAND
DRY SAND
DRY SAND
DRY SAND
DKY SAND
DRY SAND
DRY SAND
DRY SAND
6000
8000
6000
3000
4000
3000
4000
4000
4000
4000
SOIL
DENSITY
(LBS/FT3)
100
90
100
90
90
90
90
90
90
90
UNLOADED
FIELD LABOR
WAGE RATE
($/MH)
6.08
8.68
5,55
6.88
8.61
6,89
8.23
6.81
6.45
7.17
SHOP FABRICATION
vs.
FIELD ERECTION
(FT DIA)
13,5
13,5
13.5
13,5
14.5
15,0
15.0
15,0
14.5
14.5
165
-------
APPENDIX C
FROST DEPTH
166
-------
APPENDIX D
ISOTACH
167
-------
APPENDIX E
SELECTED MATERIAL COSTS
The following table lists some approximate prices for equipment item materials of
construction.
MATERIAL
APPROXIMATE
COST*
BASE MATERIAL
ALUMINUM
BERYLLIUM
BRASS
BRONZE
CARBON STEEL
COLUMBIUM
COPPER
CUPRONICKEL
GOLD
MAGNESIUM
MOLYBDENUM
MONEL
MUNTZ
NICKEL
PALLADIUM
PLATINUM
RHODIUM
SILVER
STAINLESS STEEL
TANTALUM
TIN
TITANIUM
ZINC
ZIRCONIUM
0.40
500.00
0.90
0.95
0.07
50.00
1.00
1.20
500.00
0.70
30.00
1.90
0.85
2.20
550.00
1800.00
3000.00
24.00
0.25
70.00
1.70
2.00
0.25
16.00
- 0.60
- .11
- 2.00
- 1.20
- 4.00
*3RD QUARTER 1972
168
-------
APPENDIX F
CROSS REFERENCE INDEX
TO FINU
LOOK UNDtR
IN
SECTION
ABSORBENTS
ABSORBERS/ABSORPTION TOWERS
ABSORBERS
ABSORBER-CONCENTRATOR
ACCUMULATORS
ACID EGSS
ACIOULATOHS
ADSORBENTS
ADSORPTION COLUMN
AFTERCOOLERS
A66LOMERATORS
AGITATED KETTLE
AGITATED OPEN TANKS
AGITATED PRESSURE TANKS
AGITATED VESSELS
AIR-CONDITIONERS
AIR CONDITIONING UNITS
AIH DRYERS
AIR FAN
AIR FIN
ALKYLATION REACTOR
ALKYLATORb
ATMOSPHERIC FILTRATION
AUTOCLAVES
AZEOTROPIC DISTILLATION SYSTEM
SEE ADSOKBENTS
SEE COLUMNS
SEE PACKED COLUMNS. ION EXCHANGERS-
PACKINGS
PACKED COLUMN TW
PACKING TW
SEE RECEIVER. VESStL
SEE VESSELS. REACTORS. TANKS
SEE REACTORS. VESSELS
PACKING TW
ION EXCH/.NGER IF
PACKED COLUMN TW
TRAY TOWER TW
PACKING TW
HEAT EXCHANGER HE
SEE KILNS. MILLS
AGITATED OPEN TANKS ftOT
AGITATED PRESSURE TANKS "PT
SEE ALSO REACTORS
MIXER TANK «OT
OPEN TOP TANK AOT
SEE ALSO VESSELS. REACTORS
AUTOCLAVE »PT
REACTOR APT
SEE ALSO VESSELS. REACTORS
."'JITATED OPEN TANK HOT
AGITATED PRESSURE TANK iPT
SEE ALSO AGITATORS. BLENDERS. MIXERS.
KNEADEHS. TRAY DRYING SYSTEMS.
DRYERS. ROTARY DRYERS. MILLS
AIR CONDITIONING UNITS ACU
AIR CONDITIONING SYSTEM ACU
WINDOW VENTED AIR CONDITIONER ACU
ROOFTOP AIR CONDITIONER ACU
FLOOR MOUNTED AIR CONDITIONER ACU
SEE ALSO REFRIGERATION UNITS
AIR DRYER «D
SEE ALSO ION EXCHANGER. PACKED COLUMN.
DRYERS
AIR COOLER HE
AIR COOLER HE
SEE HORIZONTAL TANKS' AGITATORS/
REACTOKS
SEE REACTORS
DUST COLLECTOR "C
FILTER F
AUTOCLAVE 1PT
SEE DISTILLATION SYSTEM
B
HAFFLE-TOWER EXTRACTORS
BAG FILTERS
BAGGER
8A6HOUSE
BEATERS
BELT FEEDERS
BIN
BIO-OXIDATION UNITS
BIOLOGICAL WASTE UNITS
BLENDERS
BLOWERS
BOILERS
BRIDGE BREAKER
BUBBLE CAPS
BUCKETS
SEE PACKED COLUMNS. TRAY TOWERS
SEE DUST COLLECTORS
PACKAGING MACHINE
CLOTH BAY DUST COLLECTOR
AUTOMATIC CLOTH L>UbT COLLECTOR
KNEAKER
MIXER
APRON COi.VEYOR
STORAGE TANK
LIGHT GAt>E TANK,
CONE ROOh TANK
CONICAL IANK
FLOATING ROOF TANK
LIFTER ROOF TANK
SEE ALSO TANK. VESSEL. RECEIVER
SEE UNUEU SPECIFIC ITEM
SEE UNDEK SPECIFIC ITEM
ULENDER
ROTARY DOUBLE-CONE yLENDER
RIBBON BLENDER
SEE ALSO KNEADERS. MIXERS
FAN
bOILER
FEEuER
BUBBLE CAP TRAY TOWER
SEE ELEVATORS. CONVEYORS
PKG
OC
OC
K
"IX
^0
VT
VT
VT
VT
VT
VT
HL
FN
WTS
PE
TW
169
-------
CALANDR1AS
CALCINERS
CANNED-MOTOR PUMPS
CATALYST
CATALYST BED REACTORS
CENTRIFUGAL PUMPS
CENTRIFUGAL CLASSIFIERS
CENTRIFUGAL EXTRACTOR
CENTRIFUfaHL FANS
CENTRIFUGAL FILTERS
CENTRIFUGAL SEPARATOR
CENTRIFUGAL SETTLERS
CENTRIFUGAL WET COLLECTOR
CENTRIFUGALS
CENTRIFUGLS
CHAIN CONVEYORS
CHEMICAL REACTORS
CHILLERS
CHIMNEYS
CHUTES
CLARIFIERS
CLASSIFIERS
CLARIFIER
COILS
COLLECTION SYSTEM
COLLECTORS
COLUMNS
COMBUSTION EQUIPMENT
COMBUSTION UNITS
COMMINUTOR
COMPACTORS
COMPOUNDERS
COMPRESSED AIR SYSTEMS
COMPRESSORS
COMPRESSORS. AIR
SHELL + TUBE CALANURIA HE
SEE ALSO HEAT EXCHANGER. EVAPORATOR
SEE ROTARY DRYERS
GEAR PUMPS GP
PACKING TW
PACKED COLUMN TW
ALSO SEE TOWERS. REACTORS. VESSELS
MODERATE SERVICE CLOSED IMPELLER CP
HEAVY DUTY SERVICE CLOSED IMPELLER CP
GENERAL SERVICE CLOSED IMPELLER CP
GENERAL SERVICE OPEN IMPELLER CP
AMERICAN VOLUNTARY STANDARD CLOSED
IMPELLER CP
CLOSED IMPELLER CP
CENTRIFUGAL PUMP TURBINE DRIVER CP
CENTRIFUGAL PUMP MOTOR DRIVER CP
SEE ALSO PUMPS. FANS. COMPRESSORS
CENTRIFUGAL PRECIPITATOR DC
CYCLONE DUST COLLECTOR DC
MULTI-CYCLONE DUST COLLECTOR DC
CONTINUOUS CENTRIFUGAL EXTRACTOR EX
ALSO SEE CENTRIFUGES
FANS FN
FILTERS F
CENTRIFUGES CT
DUST COLLECTORS DC
CYCLONE UUST COLLECTOR DC
CENTRIFUGE CT
CENTRIFUGES CT
DUST COLLECTORS DC
CENTRIFUGAL PRECIPiTATOR DUST COLLECTOR DC
SEE CENTRIFUGES. FLOATATION MACHINES.
CRYSTALLIZERS. COMPRESSORS
A.T.M. SUSPENDED CENTRIFUGE CT
SOLID BOvvL CENTRIFUGE CT
RECIPROCATING CONVEYOR CENTRIFUGE CT
SCROLL CONVEYOR CENTRIFUGE CT
HIGH SPEtD DISK CENTRIFUGE CT
HIGH SPEtD TUBULAR CENTRIFUGE CT
BATCH AUTOMATIC CENTRIFUGE CT
SUPER D HYDRATOR CENTRIFUGE CT
BATCH TOP SUSPENDED CENTRIFUGE CT
BATCH BOTTOM SUSPENDED CENTRIFUGE CT
BATCH BOTTOM DRIVEN. TOP UNLOADING CT
CENTRIFUGE
BATCH BOTTOM DRIVEN, BOTTOM UNLOADING
CENTRIFUGE CT
SEE ALSO FLOATATION MACHINES
CONVEYORS CO
REACTORS
HEAT EXCHANGER HE
REFRIGERATION UNITS RU
CONDENSERS C
FREEZERS FR
STACK <;TK
CONVEYOR CO
FILTER F
THICKENER T
FILTERS F
CENTRIFUGES CT
DUST COLLECTORS OC
SEE SCREENS
THICKENER T
PLATE COIL HEAT EXCHANGER HE
SPIRAL COIL HEAT EXCHANGER HE
SEE ALSO HEAT EXCHANGERS
DUST COLLECTOR DC
SEE DUST COLLECTORS, FILTERS
PACKED COLUMN TW
TRAY TOWERS TW
WASHERS DC
ALSO SEE VESSELS
FURNACES FU
HEATING UNITS HU
STACKS STK
SEE ALSO DRYERS, RoTARY DRYERS,
FIRED PROCESS EQUIPMENT
CUTTER CU
MILL M
SEE PRESSES
SEE PRESSES
SEE COMPRESSORS
SEE AIR COMPRESSORS, SAS COMPRESSORS.
FANS, TURBINES
SINGLE RtCIPROACATINS - ONE STAGE AC
SINGLE RECIPROCATING - TWO STAGE AC
SINGLE RECIPROCATING - THREE STAGE AC
DUPLEX RECIPROCATING - TWO STAGE »C
CENTRIFUGAL TURBINE DRIVE AC
CENTRIFUGAL MOTOR DRIVE AC
RECIPROCATING GAS ENGINE DRIVE AC
RECIPROCATING MOTOR DRIVE AC
SEE ALSO GAS COMPRESSORS, FANS
170
-------
COMPRESSORS. GAS
CONCENTRATORS
CONDITIONERS
CONDITIONING TANK
CONDENSERS
CONICAL HOPPER
CONTACTOR
CONVERTERS
CONVEYOR bELTS
CONVEYORS
COOKERS
COOLERS
COOLING TOWtRS
COOLING WATER SYSTEM
CRUSHEHS
CRACKERS
CRACKING FURNACES
CRYOGENIC UNITS
CRYSTALLI2ERS
CUTTER
CRUSHING KOLLS
CYCLONE SCRUBBER
CYCLONE VESSEL
CYCLONES
CYLINDERS
RECIPROCATING GAS ENGINE DRIVE GC
RECIPROCATING MOTOR DRIVE GC
CENTRIFUGAL TURBINt. DRIVE COMPRESSOR GC
CENTRIFUGAL MOTOR DRIVE COMPRESSOR GC
RECIPROCATING COMPRESSOR GC
SEE ALSO AIR COMPRESSORS. FANS
THICKENER T
REACTOR APT
SEE AIR CONDITIONING UNITS. WATER TREAT-
MENT SYSTEMS
SEE REACTOR. VESSEL. BIN. TANK
BAROMETRIC CONOENStR C
SEE ALSO HEAT EXCHANGERS
CONE ROOF VERTICAL TANK VT
LIGHT GAGE VERTICAL TANK VT
CONICAL TANK VT
PACKED COLUMN TW
ION EXCHANGER IE
EXTRACTOR EX
SEE REACTORS. VESStLS
CONVEYOR CO
CENTRIFUGAL BUCKET ELEVATOR CO
CONTINUOUS BUCKET LLEVATOR CO
PNEUMATIC CONVEYING SYSTEM CO
ROLLER CONVEYOR CO
SCREW CONVEYOR CO
VIBRATING CONVEYOR CO
SPACED BUCKET ELEV«TOR co
APRON CONVEYOR fO
OPEN BELT CONVEYOR TO
ENCLOSED BELT CONVEYOR CO
SEE ALSO ELEVATORS
SEE ORYEKS. TRAY DRYING SYSTEMS.
DRUM DRYERS. ROTARY DRYERS
SEE HEAT EXCHANGERS
COOLING TOWER TW
COOLING TOWER SYSTEMS WTS
COOLING TOWER TW
COOLING TOWER SYSTtM WTS
PUMP P
PUMPING STATION WTS
CONE CRUSHER CR
GYRATORY CRUSHER CR
JAW CRUSHER CR
ROLL CRUSHER CR
ROTARY CRUSHER CR
PULVERIZLR CR
SAWTOOTH CRUSHER CR
SEE ALSO MILLS. CUTTERS
FLUIDIZED BED REACTOR R
SEE ALSO REACTORS. VESSELS. TOWERS
SEE FURNACES. CRACKERS. HEATING UNITS
SEE UNOEK SPECIFIC ITEM
MECHANICAL CRYSTALLIZER CRY
OSLO GROnTH TYPE CKYSTALLIZER CRY
BATCH VACUUM CRYSTALLIZER CRY
FORCED CIRCULATION CRY
ROTARY KuIFE CUTTER CU
SEE ALSO MILLS
CRUSHER CR
ROLL MILL M
CYCLONE DC
MULTI CYCLONE OC
SEE CYCLONES
CYCLONE OUST COLLECTOR OC
MULTI-CYCLONE DUST COLLECTOR DC
SEE COLUMNS. VESSELS
DEAERATOKS
DEBUTANIZERS
DECANTER
DECOLORIZERS
DECOMPOSERS
DEDUSTERS
DEFIBERIZtRS
DEFLOCCULATORS
DEFOAMtRS
DEGAS1FIERS
DEGUMMERS
DEHUM1L/IFIERS
DEHYDRATORS
DEIONIZERS
DEISOBUTINIZERS
DEISOPENTANIZERS
DELUMPERS
SEE MIXLKS
SEE DISTILLATION SYSTEMS
SUPER D CENTRIFUGE CT
SEE ALSO SEPARATOR
SEE ABSORBERS.ACTIVATED CARBON
SEE AGITATED VESSELS
SEE DUST COLLECTORS
SEE CRUSHERS/MILLS
SEE CRUSHERS/MILLS
SEE MIXERS
SEE DEAEkATORS/MIXtRS
SEt CENTRIFUGES. EVAPORATORS.
WIPED FILM EVAPORATORS
DRYERS n
AIR CONDITIONING UNIT "CU
AIR DRYEKS . AD
SEE DISTILLATION SYSTEMS. DRYERS. ROTARY
DRYERS. TRAY DRYING SYSTEMS. EVAPORAT-
ORS. WIPED FILM EVAPORATORS. DRUM
DRYERS. FLAKERS
SEE ION-EXCHANGERS. SOFTENERS
SEE DISTILLATION SYSTEMS
SEE DISTILLATION SYSTEMS
SEE CRUSHERS. MILLS. MIXERS
171
-------
DEMINERALIZER
DENSIFIERS
DEODORIZERS
DEPROPANUERS
DESICCATORS
OESILICIZERS
DESICCANTS
DESICCATORS
DESILTERS
DESLUD6ERS
OESMOGGERS
DESOUVENTIZERS
OESORbERS
DESTRUCTORS
OESULFURIZATION REACTOR
DEWATERERS
DEWATERING StSTEM
DEWATERINS SYSTEM
DIFFUSEKS
DIGESTERS
DISPERSERS
DISPOSAL UNITS
DISSOLVES
DISTILLATION EQUIPMENT
DISTILLATION UNITS
DISTILLATION SYSTEM
DISTILLED WATER SYSTEM
DRUM
DRAINERS
DRIVES
DRYING SYSTEM
DRY CHEMICAL FEEDER
DRYERS
OUST COLLECTORS
DRUM DRYERS
DUST COLLECTION SYSTEM
WATER TREATMENT SYSTEM WTS
ION EXCHANGER IE
PACKED COLUMN TW
PACKING TW
SEE MIXERS
SEE REACTORS> DISTILLATION SYSTEMS'
DRYERS
SEE DISTILLATION SYSTEMS
SEE ION EXCHANGERSi PACKED COLUMNSr
PACKINGS
SEE ION-EXCHANGERS
SEE PACKINGS
SEE DRYERS. PACKED COLUMNS. PACKINGS
VIBRATING SCREEN VS
SEE CENTRIFUGES. FILTERS. THICKENERS
SEE DUST COLLECTORS. FILTERS
SEE DRYERS. DRUM DRYERS. TRAY DRYING
SYSTEMS. ROTARY DRYERS. EVAPORATORS.
DISTILLATION SYSTEMS
SEE COLUMNS. TOWERS. VESSELS. REACTORS -
SEE INCINERATORS
PACKED COLUMNS TW
SEE ALSO REACTORS. TOWERS. VESSELS
SEE CENTRIFUGES. FILTERS. DRYERS.
ROTARY DRYERS. TURBO DRYING SYSTEMS
CONVEYOR CO
VIBRATING SCREEN VS
ROTARY VACUUM FILTER F
CENTRIFUGAL PUMP CP
PUMP P
DUST COLLECTOR DC
AIR DRYER AD
DRYING SYSTEM
INCINERATOR I
RECEIVER
VACUUM PUMP VP
FILTER F
HOPPER
SEE MIXEkS
SEE REACTORS. VESSLLS
SEE MIXERS. BLENDERS. AGITATORS
SEE UNDER SPECIFIC ITEM
SEE MIXERS
SEE UNDER SPECIFIC ITEM
SEE DISTILLATION SYSTEMS
TRAY TOWER TW
PACKED COLUMN TW
HEAT EXCHANGER HE
REBOILER RB
CONDENSER C
PUMP P
CENTRIFUGAL PUMP CP
VACUUM PUMP VP
STILL WTS
SEE ALSO RECEIVER
STILL WTS
SEE ALSO DISTILLATION SYSTEM
SEE BIN. RECEIVER. DRUM. VESSEL
SEE CENTRIFUGALS
SEE TURBINES
DRYER n
ROTARY DRYER RD
TRAY DRYING SYSTEM TDS
DRUM DRYLR DD
FEEDER P
CONVEYOR CO
ATMOSPHERIC TRAY DRYER 0
VACUUM TRAY DRYER n
PAN DRYER D
SPRAY DRYER 0
FLUID BEu DRYER n
ALSO SEE ROTARY ORYERSi DRUM DRYERS.
TRAY DRYING SYSTEMS' FLAKERS
CLOTH BAY DUST COLLECTOR PC
CYCLONE COLLECTOR DC
MULTIPLE CYCLONE COLLECTOR DC
WASHERS DC
AUTOMATIC CLOTH FILTER DUST COLLECTOR DC
LOW VOLTAGE ELECTRICAL PRECIPITATOR DC
HIGH VOLTAGE ELECTRICAL PRECIPITATOR DC
CENTRIFUGAL PRECIPITATOR DC
SEE ALSO FILTERS. SEPARATORS
SINGLE ATMOSPHERIC DRUM DRYER HD
DOUBLE ATMOSPHERIC DRUM DRYER DD
SINGLE ATMOSPHERIC DRUM DRYER DD
SEE ALSO DRYERS" FLAKERS. ROTARY DRYERS -
DUST COLLECTOR DC
FAN FN
ECONOMIZER
HEAT EXCHANGER
EVAPORATOR
HE
E
172
-------
EDUCATORS
ELECTRICAL GENERATORS
EJECTORS
ELECTROSTATIC PRECIPITATOR
ELEVATORS
EMULSIFIEKS
ENGINES
EVACUATORS
EVAPORATORS
EXCHANGE RESIN
EXCHANGER
EXTRACTORS
EXHAUSTERS
EXTRACTORS
EXTRACT FURNACES
EXTRACTION COLUMNS
EXTRUDERS
CONDENSER C
REBOILER RB
BOILER
EJECTOR F-J
STEAM JET REFRIGERATION UNIT RU
TURBO GENERATOR EG
UNIT STEAM AND BOILER EG
PORTABLE GENERATOR SET EG
SEE ALSO TURBINES
SINGLE STAGE NON-CONDENSING EJECTOR EJ
TWO STAGE - BAROMETRIC TYPE OF INTER- EJ
CONDENSER FJ
FOUR STAGE - BAROMETRIC EJ
FIVE STAGE - BAROMETRIC EJ
SEE ALSO REFRIGERATION UNITS. VACUUM
PUMPS
DUST COLLECTOR OC
PASSENGER ELEVATOR EL
FREIGHT ELEVATOR FL
SEE ALSO CONVEYORS
SEE MIXEKS
SEE ALSO SEPARATORS
SEE TURBINES. ELECTRICAL GENERATOR
UNITS
SEE EJECTORS
AGITATED FALLING FILM EVAPORATOR E
FORCED CIRCULATION EVAPORATOR E
LONG-TUBE RISING FILM EVAPORATOR E
STANDARD HORIZONTAL TUBE EVAPORATOR E
STANDARD VERTICAL TUBE EVAPORATOR E
JACKETED VESSEL TYPE EVAPORATOR E
LONG TUBL VERTICAL EVAPORATOR E
SEE ALSO WIPED FILM EVAPORATORS. HEAT
EXCHANGERS- FURNACES. HEATING UNITS
PACKING TW
BACKED COLUMN TW
ION EXCHANGER IE
HEAT EXCHANGER HE
REBOILER RB
EVAPORATOR F.
CONUENSEK
CONTINUOUS CENTRIFUGAL EXTRACTOR EX
SEE ALSO CENTRIFUGtS
SEE BLOWtRS. FANS' VACUUM PUMPS'
COMPRESSORS' EJECTORS. GEAR PUMPS.
CENTRIFUGAL PUMPS
EXTRACTOR EX
AGITATED PRESSURE TANKS APT
CENTRIFUGE CT
SEE FURNACES. HEATING UNITS
SEE AGITATED VESSELS. VESSELS. REACTORS -
MIXLR MX
FANS
FEED HEATER
FEED PUMP
FEED TANK
FEEDERS
FIBERUERS
FIELD EREt-TED VESSELS
FILTER BAoS
FILTER CLOTHS
FILTER LEAVES
FILTER PRESSES
CENTRIFUGAL TURBO BLOWER FN
CENTRIFUGAL COMPRESSOR FN
PROPELLER FAN FN
ROTARY BLOWER FN
VANEAXIAL FAN FN
CENTRIFUGAL FAN FN
SEE ALSO GAS COMPRESSORS. AIR COMPRESS-
ORS. PUMPS
SEE HEATERS
SEE PUMP
SEE TANK. VESSEL
bELT FEEDER FE
CHAMBER FEEDER FE
LOSS IN WEIGHT FEEDER FE
ROTARY FEEDER FF
SEE ALSO CONVEYORS
StE MILLS
SPHERES VT
SPHEROIDS VT
CONE ROOF TANKS VT
CONICAL TANKS VT
FLOATING ROOF TANKS VT
LIFTER ROOF TANKS VT
GAS HOLDERS VT
OPEN TOP TANKS VT
AGITATED OPEN TANKS
-------
FILTER SCREENS
FILTER UNIT
ULTERS
FILTRATE RECEIVERS
FILTRATE TANK
FILTRATION
FINISHER
FINISHING
FIRED PROCESS EQUIPMENT
FIRED ROTARY KILN
FLAKERS
FLOATATION MACHINES
FLASH DRUM
FLASH TOWLRS
FLOTATION UNITS
FLUE 6AS SCRUBBING SYSTEM
FLUIOIZEU BED REACTOR
FLUIDIZING CONVEYOR SYSTEMS
FLOTATION UNITS
FRACTIONATORS
FRAME FILTER
FREEZERS
FUME COLLECTORS
FUME EXHAUST SYSTtMS
FUMI6ATORS
FURNACES
VIBRATING SCREENS VS
FILTER F
SE£ ALSO SEPARATORS
SPARKLER FILTER F
ROTARY DhUM FILTER F
ROTARY DISK FILTER F
PLATE AND FRAME FILTER F
PRESSURE LEAF-DRY FILTER F
PRESSURE LEAF-vfET FILTER F
SEWAGE FILTER SYSTEM F
SEE ALSO DUST COLLECTORS> SEPARATORS
SEE RECEIVERS
SEE TANK. VESSEL. RECEIVER
FILTER F
DUST COLLECTOR DC
WIPED FILM EVAPORATOR WFE
EVAPORATOR E
DRUM DRYER DD
ALSO SEE TUBULAR REACTOR. REACTOR
SEE MILLS
FURNACES FU
HEATING UNITS HU
BOILERS WTS
STACKS STK
DRYERS 0
ROTARY OhYERS 90
STILL WTS
ROTARY DRYER RD
DRUM FLAKER FL
DRUM DRYER OD
SEE ALSO DRUM ORYERS
FLOATATION MACHINE FM
SEE ALSO CENTRIFUGES
SEE DRUMb. VESSELS. REACTORS. TANKS
SEE TOWERS
FLOATATION MACHINE CM
SCRUBBER
DUST COLLECTOR PC
FILTER F
FAN FN
PACKED COLUMN TW
PACKING TW
FLUIDIZEu BED REACTOR R
SPHERES VT
SPHEROIDS VT
ION EXCHANGERS IE
WASHERS DC
SEE CONVEYORS
SEE FLOATATON MACHINE. THICKENER'
REACTORS
SEE DISTILLATION SYSTEMS
PLATE ANb FRAME FILTER PRESS F
FREEZER FR
SEE ALSO REFRIGERATION UNITS. AIR
CONDITIONING UNITS
DUST COLLECTOR DC
SEE PUMPS. FANS
SEE VESSELS
PROCESS HEATER FURNACE FU
VERTICAL FURNACE FU
bOX FURNACE PU
PYROLYSIS FURNACE FU
REFORMER FURNACE FU
SEE ALSO HEATING UNITS
GAS CONVEYING SYSTEM
GAS ABSORBER
SASHOLOERS
GAS SCRUBBER
GEAR PUMPS
GAS »
-------
H
HALOGENATORS
HAMMERMILLS
HEAT EXCHANGERS
HEAT RECOVERY UNITS
(EAT TRANSFER SYSTEM
HEATERS
HEATING UNITS
HIGH-EFFICIENCY CENTRIFUGAL
COLLECTOR
HIGH EFFICIENCY CYCLONE
HIGH VELOCITY SCRUBBER
HOISTS
HOLDING TANK
HOMOGENIZERS
HOPPLR
HORIZONTAL PLATE FILTER
HORIZONTAL TANKS
HYDRAULIC CONVEYOR SYSTEMS
HYDRO-EXTRACTORS
HYDROGENATION REACTOR
SEE MIXEhS
SEE CRUSHERS. MILLS
SHELL ANU TUBE HEAT EXCHANGER HE
SHELL ANL, TUBE CALANDRIA HE
GLASS COIL IN GLASS SHELL EXCHANGER HE
FLOATING HEAD TYPE HEAT EXCHANGER HE
FIXED TUbE SHEET TYPE HEAT EXCHANGER HE
U-TUBE TYPE HEAT EXCHANGER HE
TANK HEATER - STEAM COIL HE
TANK HEATER - IMMERSION HE
JACKETED PIPE EXCHANGER HE
TANK SUCTION HEATER HE
TWIN SCRtW HE
THERMASCKEW (RIETZ) SINGLE SCREW HE
TWIN SCREW AGITATED AND JACKETED HE
WASTE HEAT BOILER HE
CASCADE COOLER HE
PLATE COIL HEADER TYPE SERPENTINE TYPE HE
DRIP COOLER HE
FIN TUBE EXCHANGER HE
AIR COOLnR HE
U-TUBE HEAT EXCHANGER HE
SPIRAL TU8E HEAT EXCHANGER HE
SPIRAL PLATE HEAT EXCHANGER HE
SEE ALSO HEATING UNITS. EVAPORATORS.
FURNACES. REFRIGERATION UNITS.
CONDENSERS. FREEZERS. AIR CONDITIONING
UNITS
SEE FURNaCES. HEATING UNITS. BOILERS.
• HEAT EXCHANGERS
HEAT EXCHANGER HE
CONDENSER C
REBOILER PR
EVAPORATOR F
HIIPED FILM EVAPORATOR WFE
COOLING TOWER SYSTEM WTS
COOLING 10WER TW
HEATING UNIT HIJ
FREEZER FR
FURNACE FU
AIR COOLtR HE
REFRIGERATION UNIT RU
ALSO SEE DRYER. REFRIGERATION SYSTEM
SEE FURNACES. HEATING UNITS. HEAT
EXCHANGERS
UOWTHERM HU
PROCESS HEATER TYPE HEATING UNIT HU
SEE ALSO FURNACES
MULTI CYCLONE DUST COLLECTOR DC
CYCLONE DUST COLLECTOR OC
MULTI CYCLONE OUST COLLECTOR DC
WASHER DC
SEE ALSO SCRUBBER
5-SPEED ELECTRIC HOIST WITH MOTOR
DRIVE TROLLEY HO
HAND HOIST. PLAIN TROLLEY HO
HAND HOIST. GEARED TROLLEY HO
HAND HOIST. NO TROLLEY
SINGLE-SPEED ELECTRIC HOIST. NO TKOLLFY HO
5-SPEED ELECTRIC HOIST. NO TROLLEY HO
SEE ALSO CRANES
SEE VESSEL. TANK. BIN. DRUM
SEE MIXERS
SEE BIN. TANK. VESSEL. RECEIVER
SPARKLER FILTER F
VACUUM RECEIVER HT
JACKETED VACUUM RECIEVER HT
CYLINDRICAL VESSEL HT
SPHERE VT
STORAGE TANK VT
SPHEROID VT
SEE ALSO VESSELS. TANKS
PNEUMATIC CONVEYOR SYSTEM CO
SEE CENTRIFUGALS
PACKED COLUMN TW
IMPACTORS
IMPELLERS
IMPREGNATORS
INCINERATION SYSTEM
SEE CRUSHERS. MILLS
SEE AGITATORS. MIXERS
SEE VESStLS
INCINERATOR
STACK
I
STK
175
-------
INCINERATORS
INTENSIFItRS
INTERCOOLERS
INERTIAL »ET COLLECTOR
ION EXCHANGERS
ION-EXCHANGE RESINS
ION RETARDATION UNITS
1SOMERIZATION REACTORS
ISOSTRIPPER
FAN F.N
CONVEYOR CO
TANK
INCINERATOR I
MIXERS MX
BLENDERS BL
KNEADERS K
SEE HEAT EXCHANGERS, AIR DRYERS
CENTRIFUGAL PRECIPITATOR DUST COLLECTOR DC
ANION TYPE ION EXCHANGER
HYDROGEN CYCLE CATION TYPE ION
EXCHANGER IE
SODIUM CYCLE CATION TYPE ION EXCHANGER IE
SEE ALSO PACKED COLUMNS, WATER TREAT-
MENT SYSTEMS
PACKING TW
SEE ALSO ION EXCHANGERSi PACKED COLUMS -
SEE ION EXCHANGERS- REACTORS
SEE DISTILLATION SYSTEMS
SEE DISTILLATION SYSTEMS
JACKETED REACTOR
JET VACUUM EQUIPMENT
REACTOR
EJECTORS
STEAM JET REFRIGERATION UNIT
FJ
RU
KETTLES
KILNS
KNEADERS
KNOCK-OUT DRUM
KYMER DIGESTER
SEE REACTORS, REbOlLERS
CRYSTALLIZERS
SEE ROTARY DRYERS
STATIONARY, UPRIGHT DOUBLE-ARM KNEADER K
TILTING, DOUBLE-ARM KNEADER K
VACUUM, TILTING-TYPE DOUBLE-ARM KNEADER K
SEE ALSO BLENDERS, MIXERS
HORIZONTAL TANKS HT
VERTICAL TANKS VT
ALSO SEE VESSELS, TANKS
SEE REACTOR, VESSEL
LEACHERS
LOADER
SEE VESSELS, REACTORS
FEEUER
CONVEYOR
HOIST
ELEVATOR
FE
CO
HO
FL
MAIN COLUMN
MAIN FRACTIONATORS
MAKE-UP AIR UNITS
MAKEUP COMPRESSOR
MANCOOLERb
MASTICATORS
MECHANICAL COLLECTOR
METERING PUMP
METHANATOKS
MICRON1ZERS
MIX-COOKES
MILLS
MIXERS
MULTI-STAGE PUMP
MULLEHS
SEE TOWERS
SEE DISTILLATION SYSTEMS
SEE BLOWERS, FANS, COMPRESSORS
COMPRESSORS
SEE FANS, AIR CONDITIONING UNITS
SEE MIXERS, AGITATORS, BLENDERS
DUST COLLECTOR DC
PUMP P
GEAR PUMP RP
SEE TOWERS, COLUMNS, VESSELS, REACTORS -
SEE MILLS, CRUSHERS
SEE DRUM DRYER, DRYER, MIXER,
TURBO DRYING SYSTEM
ATTRITION MILL M
SWING HAMMER MILL M
MIKRO-PUUVERIZER "
ROLLER MILL M
BALL MILL M
HAMMER MILL M
SEE ALSO CRUSHERS
SIGMA MIXER
FIXED PROPELLER MIXER
PORTABLE PROPELLER MIXER
EXTRUDER-STEEL CYLINDRICAL VARIABLE MX
DRIVE
EXTRUDER-MULLER MX
SPIRAL RIBBON MIXER MX
TWO-ROLL MIXER MX
PAN MIXER MX
AGITATED OPEN TANK AOT
AGITATED PRESSURE TANK APT
ROTARY BLENDER BL
RI'BBON BLENDER RL
BLENDER PL
SEE ALSO BLENDERS,KNEADERS, AGITATORS
CENTRIFUGAL PUMP CP
PUMP P
SEE MIXEHS
176
-------
N
NEUTRALIZtRS
NITRATORS
NODUL1ZERS
SEE M1XEKS' VESSELS. REACTORS
REINFORCED CONCRETE ITEM
SEE VESSELS' REACTORS
SEE KILNS
OXIUIZEH
SEE REACTORS' VESSELS' COLUMNS' TOWERS -
PACKAGING EQUIPMENT
PACKAGING MACHINES
PACKED COLUMN
PACKERS
PACKING
PANS
PANEL FILTER
PASTEURIZtRS
PELLETIZEKS
PERCOLATOKS
PILOT-SCALE EQUIPMENT
PIPELINE REACTOR
PLATE COILS
PLATE TOWER
PNEUMATIC CONVEYOR SYSTEMS
POLYMERIZtR
POTS
POWER RECOVERY TURBINES
PREBREAKERS
PREC1PITATORS
PREHEAT FURNACE
PREHEATERS
PRESSES
PRESCRUBbLR
PRESSURE FILTER
PRIMARY CLARIFIER
PROCESS COOLERS
PROCESS HEATER
PROCESSORS
PRODUCT PUMP
PRODUCT TrtNK
PROPANE ACCUMULATORS
PULP DIGESTER
PUMPS
PUMPING STATION
PUMPING SYSTEMS
PURIFIERS
PURIFICATION SYSTEM
VOLUME BAGGER °KG
WEIGHT B,,6GER PKG
BAGGING MACHINE PACKED BY WEIGHT PKG
BAGGING MACHINE PACKED BY WEIGHT "KG
PACKED COLUMN TW
SEE PACKAGING EQUIPMENT
SEE UNDER SPECIFIC ITEM TW
SEE ALSO PACKED COLUMNS. ION EXCHANGERS -
PAN MIXER MX
HAN DRYER 0
CLOTH BAY OUST COLLECTOR nc
AUTOCLAVES ^PT
SEE ALSO VESSELS' REACTORS
ROTARY KNIFE CUTTEK CU
SEE VESSELS' REACTuRS
SEE UNDER SPECIFIC ITEM
JACKETED PIPE HEAT EXCHANGER HF
ALSO SEE TUBULAR REACTORt HEAT
EXCHANbER' REACTOR
PLATE COIL HEAT EXCHANGER HE
TRAY TOWER TW
PNEUMATIC CONVtYINo SYSTEM CO
SEE ALSO FANS' COMPRESSORS! YARD PIPE
AGITATED PRESSURE TANK KPT
WIPED FILM EVAPORATOR WFE
ALSO SEE REACTOR. TUBULAR REACTOR
SEE VESSELS' REACTURS. TANKS. DRUMS
TURblNE TUR
ELECTRICAL GENERATOR FG
SEE CRUSHERS. MILLS
SEE TANKS' THICKENERS
SEE FURNHCES. HEATING UNITS
SEE HEATtRS
HYDRAULIC. PRESS PR
SEE SCRUbBER
FILTER F
ALSO SEE SEPARATOR
THICKENEK T
SEE HEAT EXCHANGERS. COOLING TOWER
SYSTEMS
HEAT EXCHANGER HE
FURNACE FU
HEATING UNIT HU
SEE REACTORS' DRYING SYSTEMS
SEE PUMP
SEE TANK. VESSEL' RECEIVER
SEE ACCUMULATORS
SEE REACTOR' VESSEL
RECIPROCATING - SIMPLEX. STEAM DRIVE P
RECIPROCATING - UUPLEX STEAM DRIVE P
TRIPLEX OR PLUNGER MOTOR DRIVE P
DIAPHRAGM TFE TYPE SLURRY TYPE P
ROTARY PUMP P
GEAR PUMP P
SEE ALSO GEAR PUMPS. CENTRIFUGAL PUMPS'
VACUUM PUMPS. FANS
CENTRIFUGAL PUMP CP
PUMP P
PUMPING STATION WTS
PUMPING STATIONS WTS
SEE ALSO PUMPS. CENTRIFUGAL
PUMPS
SEE DUST COLLECTORS. FILTERS' CENT-
RIFUGEb, DRYING SYSTEMS' DISTILL-
ATION SYSTEMS
FILTER F
CENTRIFUGE CT
DUST COLLECTOR OC
ALSO SEE SEPARATOR
177
-------
RAFFII^TE
RAILROAD TANK CARS
REACTION VESSEL
REACTORS
REbOILERS
RECEIVER
RECYCLE CLAHIFIER
REFRIGERANT CONDENSER
REACTION SYSTEMS
REACTORS
RECYCLE COMPRESSOR
REFQRMtRS
REFRIGERATION MACHINERY
REFRIGERATION UNITS
REGENERATORS
REHEATER
REPULPING VESSELS
RESIN
RETORTS
REVERSt OSMOSIS SYSTEM
RISER CRACKERS
ROASTERS
ROLLERS
ROTARY DRYERS
ROASTERS
ROTARY VACUUM FILTER SYSTEM
ROTATING DRYER
ROTARY VACUUM SYSTEM
SEE FUKN,.CES. HE»TING UNITS
CHLORINE TYPE TANK CAR RTC
SEE REACTOR i VESSEL.
AGITATED OPEN TANK ftOT
FLUIDIZEL BED SINGLE STAGE REACTOR R
FLUIDIZEU BED DOUBLE STAGE REACTOR R
AGITATED PRESSURE TANK «PT
MIXER MX
ALSO SEE REACTOR. VESSEL
KETTLE TYPE RE60ILER HE
U-TUBE RtBOILER HE
SEE ALSO HEAT EXCHANGERS. EVAPORATORS
HORIZONTAL PRESSURE VESSEL HT
VERTICAL PRESSURE VESSEL VT
ALSO SEE VESSEL. TANK. DRUM
VlBRATIMb SCREEN VS
HEAT EXCHANGER HE
REFRIGERATION UNIT RU
AIR COOLtR HF
AIR CONDITIONING U.'lIT *CU
SEE REACTORS. DISTILLATION SYSTEMS
REACTOR APT
AUTOCLAVE APT
HORIZONTAL CYLINDRICAL PRESSURE VESSEL HT
VERTICAL CYLINDRICAL PRESSURE VESSEL VT
TRAY TOWLR T«
PACKED COLUMN TW
JACKETED HORIZONTAL VACUUM VESSEL HT
JACKETED VERTICAL VACUUM VESSEL VT
/sGITATED PRESSURE VESSEL APT
AGITATED OPEN TANK AOT
COMPRESSORS
REFORMER FURNACE FU
REFRIGERATION UNIT RU
AIR CONDITIONING UNIT ACU
FREEZER FR
MECHANICAL COMPRESSION UNIT RU
STEAM JtT REFRIGERATION UNIT RU
CENTRIFUGAL COMPRESSION UNIT RU
SEE ALSO FREEZERS* AIR CONOITIONU4G
UNITS ,
SEE HEAT EXCHANGERS. VESSELS' REACTORS.
EVAPORATORS" BOILERS
SEE HEATER
SEE AGITATED VESSELS
PACKING TW
ION EXCHANGER IE
SEE DISTILLATION SYSTEMS. REACTORS
HORIZONTAL PRESSURE VESSEL HT
ALSO SEE PUMP' TUBULAR REACTOR. VFSSEL -
SEE CRACKERS
SEE KILNS. DRYERS. REACTORS
SEE MIXERS
DIRECT ROTARY DRYER RD
BATCH ROTARY VACUUrt DRYER r>D
INDIRECT ROTARY DRYER RD
SEE ALSO DRUM ORYEKS. FLAKERS. TURBO
DRYING SYSTEMS. L.RYERS
SEE DRYING SYSTEMS
ROTARY VACUUM FILTtK F
VACUUM PUMP VP
EJECTOR FJ
ALSO SEE RECEIVER. VESSEL
ROTARY DRYER RD
DRUM DRYLR DO
ALSO SEE DRYER
SEE ROTARY VACUUM FILTER SYSTEM
SAFETY EQUIPMENT
SAMPLING PUMP
SCALES
SCALPEKS
SCRAPER KETTLES
SCREEN CLOTH FILTLR
SCREEN
SCHEW DRYERS
SCREW HEATERS
SEE UNDER SPECIFIC ITEM
SEE PUMP
TANK SCALE S
SEE VIBRATING SCREENS
SEE REACTORS
ROTARY VACUUM FILTtR F
ROTARY DRUM FILTER F
ROTARY DISK FILTER F
PLATE AND FRAME FILTER PRESS F
ALSO SEE ROTARY VACUUM FILTER SYSTEM
VIBRATING SCREEN VS
SEE SCREW HEATERS
ONE SCREW THERMASCREW HE
178
-------
SCRUBBERS
SCRUBBING TOWER
SECONDARY CLARIFIER
SEPARATORS
SETTLERS
SEPARATION VESSELS
SETTLING TANK
SEWAGE PUMP
SEWAGE TREATING EQUIPMENT
SHIFT CONVERTERS
SHREDDERS
SILOS
SILO HOPPtR
SIMPLE CYCLONE
SINGLE-STAGE ELECTRICAL PRECIP-
ITATOR
SIZE REDUCTION EQUIPMENT
SOFTENERS
SOLVENT RECOVERY EQUIPMENT
SPARE PUMP
SPHERES
SPRAY CHAMBER
SPRAY CHAMBER WET COLLECTOR
SPARY MIXERS
"SPRAY TOWER
SPREADERS
STABILIZED
STACKS
STAR FEEDER
STATIONS
STEAM HEATING SYSTEM
STEAM PLANT
STERILIZERS
STILLS
STIRRED VESSEL
STRIPPtRS
SUuLIMERS
SUCTION DKUM
SULFONATION REACTOR
SULFONATOKS
SUMPS
SUPERHEATERS
SURGE BIN
SURGE HOPPER
SWING REACTOR
TWO SCREH THERMASCREW HE
SCREW CONVEYOR CO
WASHERS OC
PACKED COLUMN TW
SEE ALSO PACKING TW
TRAY TOWER TW
ALSO SEE VESSEL
SEE SCRUBBER
SEE CLARIFIER
VIBRATING SCREENS VS
FILTERS c
DUST COLLECTORS DC
THICKENER T
EXTRACTOR FX
VIBRATING SCREEN VS
ALSO SEE DISTILLATION SYSTEM' DRYER
SEE CLARIFIERS' FILTERS. DUST COLL-
ECTORS/ TANKS, VESSELS
SEE VESSELS
THICKENER T
ALSO SEE VESSEL
CENTRIFUGAL PUMP CP
ALSO SEE PUMP
SEE UNDER SPECIFIC ITEM
SEE COLUMNSr REACTORS• VESSELS
SEE CRUSHERS. MILLS. CUTTERS
SEE VESSELS
LIGHT GAGE VERTICAL TANK VT
VERTICAL STORAGE VESSEL VT
CYCLONE UU5T COLLECTOR DC
LOW-VOLTAGE ELECTRICAL PRECIPITATOR
DUST COLLECTOR DC
HIGH-VOLTAGE ELECTRICAL PRECIPITATOR
DUST COLLECTOR DC
SEE CRUSHERS. MILLS. CUTTERS, KNEADERS -
WATER SOFTENING SYSTEMS WTS
ION EXCHANGERS IE
PACKING TW
COOLING TOWER SYSTEM WTS
PACKED COLUMN TW
COOLING TOWER TW
SEE DISTILLATION SYSTEMS. DRYERS.
HEAT EXCHANGERS. TRAY DRYING SYSTEMS,
DRUM DKYERS, FILTERS
PUMP P
SPHERE VT
SPHERIOO VT
WASHER DUST COLLECTOR DC
ALSO SEE SCRUBBER. VESSEL
WASHER DUST COLLECTOR OC
SEE MIXEKS
WASHER OUST COLLECTOR DC
SEE ALSO REACTORS. VESSELS
COOLING TOWER SYSTtM WTS
COOLING TOWER TW
PACKED COLUMN I TW
ALSO SEE SCRUBBER. VESSEL
SEE CENTRIFUGALS
SEE DISTILLATION SYSTEMS
STACK STK
ROTARY FEEDER FE
PUMPING STATION WTS
tiOILER WTS
EVAPORATOR E
WATER TREATMENT SYSTEM WTS
AUTOCLAVES APT
STILL WTS
AGITATED OPEN TANK AOT
REACTOR
AGITATED PRESSURE TANK APT
THICKENER T
AGITATOR AG
SEE COLUMNS. TOWERS, DISTILLATION
SYSTEMS
TURBO TRAY DRYER TDS
VACUUM RECEIVER - HORIZONTAL HT
VACUUM RtCEIVER -VERTICAL VT
ALSO SEE VESSELS. REACTORS. DRUMS
AGITATED TANK APT
ALSO SEE VESSEL. TUBULAR REACTOR
bEE REACTORS, VESStLS
SEE VESSELS
BOILER WTS
SEE BIN
SEE VESSLLS
SEE REACTORS
179
-------
TANK STORAGE TANK VT
HORIZONTAL TANK HT
VERTICAL TANK VT
ALSO SEE BIN' URUMr VESSEL* RECEIVER
TEXTUKIZLKS SEE MIXEKS
THERMO-COMPKEbbORS SEE COMPRESSORS
THICKENERb CONTINUOUS SINGLE COMPARTMENT THICKENER T
DOU13LE COMPARTMENT THICKENER T
TOPING SECTION SEE DISTILLATION SYSTEM
TRAY DRYING SYSTEMS TURBO DRYER SYSTEM TDS
BATCH TRAY TYPE URYLR TDS
BATCH TYPE TRAY URYER TDS
ATMOSPHERIC TRAY DRYER TDS
SEE ALSO DRYERS> DRUM DRYERS) ROTARY
DKYERS
TREATING TO«iERb SEE TOWERS
TUBULAR CLOTH FILTEK CLOTH BAY DUST COLLECTOR OC
AUTOMATIC CLOTH UUbT COLLECTOR DC
180
-------
TUBES
TUMBLERS
TUBULAR RtACTOR
TUMBLE BURNER
TUMBLE DRYER
TURBINES
TURBO-COMPRESSORS
TURBO DRYING SYSTEM
TOWERS
TWO-STAGE ELECTRICAL PRECIPITATOR
SEE HEAT EXCHANGERS, EVAPORATORS
SEE MILLS, MIXERS, KNEAOERS,
BLENOEkS
HEAT EXCHANGER HE
EVAPORATOR F:
WIPED FILM EVAPORATOR WFE
CRYSTALLIZER CRY
ROTARY DrtYER RD
ROTARY DHYER RO
GAS TURBINE TUR
SINGLE STAGE STEAM TURBINE
CONDENSING TYPE TUR
SINGLE STAGE STEAM TURBINE
NON-CONDENSING TYPE
SEE ALSO ELECTRICAL GENERATOR UNITS
SEE TURBINES, COMPRESSORS
TURBO DRYER SYSTEM TDS
SEE ALSO TRAY DRYING SYSTEMS
PACKED TOWER TW
COOLING TOWER TW
OUBBLE-CHP TRAY TO«ER TW
TURBO GRID TRAY TOwER TW
SIEVE TKhY TOWER TW
WASHERS DC
SEE ALSO VESSELS, COLUMNS
LOW-VOLT,,GE ELECTRICAL PRECIPITATOR
DUST COLLECTOR OC
HIGH-VOLTAGE ELECTRICAL PRECIPITATOR
DUST COLLECTOR nc
ULTRAFILTKATION SYSTEM
UNLOADERS
UREA REACTOR
U
OSMOSIS
SEE REVEKSE OSMOSIS SYSTEM
SEE CONVtYORS, ELEVATORS
CYLINDRICAL PRESSURE VESSEL
PACKING
ALSO SEE PACKED COLUMN, VESSEL
VT
TW
VACUUM CONVEYING SYSTEMS
VACUUM EJECTOR SYSTEMS
VACUUM PUMPS
VACUUM SYSTEM
VAPORIZERS
VENT STACK
'VERTICAL TANKS
VESStLS
PNEUMATIC CONVEYING SYSTEM
SEE ALSO COMPRESSORS, FANS, VACUUM
PUMPS
EJECTORS CJ
STEAM JET REFRIGERATION UNIT RU
MECHANICAL VACUUM PUMP VP
WATER-SEALED 20 IN HG VACUUM PUMP VP
OIL-SEALED VACUUM PUMP VP
MECHANICAL BOOSTER VACUUM PUMP VP
SEE ALSO PUMPS, GEAR PUMPS
HORIZONTAL VACUUM RECEIVER HT
VERTICAL VACUUM RECEIVER VT
VACUUM PUMP VP
EJECTOR FJ
CONDENSEK r.
EVAPORATORS F
HEAT EXCHANGERS HF
WIPED FILM EVAPORATORS WFE
FURNACE FU
HEATING UNIT nu
STACK <;TK
VACUUM RECEIVER VT
CYLINDERICAL VERTICAL TANK VT
SPHERIOO VT
SPHERE VT
ASME CODE CYLINDRICAL VESSEL VT
ATMOSPHERIC STORAGE TANK VT
CONE ROOF TANK VT
OPEN TOP TANK VT
LIGHT GAGE TANK VT
GAS HOLDtR VT
JACKETED VACUUM RECEIVER VT
JACKETED VT
SILO HOPPER VT
CONICAL TANK VT
CONE ROOF TANK VT
STORAGE TANK VT
LIFTER T,,NK VT
FLOATING ROOF TANK VT
SEE ALSO VESSELS, AGITATED VESSELS
VERTICAL TANKS VT
HORIZONTAL TANKS MT
AGITATED OPEN TANKS AOT
AGITATED PRESSURE TANKS APT
TRAY TOWtRS TW
PACKED COLUMNS TW
ION EXCHANGERS IE
WASHERS DC
REACTOR R
SPHERIOO VT
181
-------
VIBRATING SCREENS
VIBRATORY SEPARATOR
SPHERE VT
THICKENERS T
SEE ALSO REACTORS' FIELD ERECTED
VESSELS' DRYERS.' FILTERS/ SCRUBBERS
SINGLE DECK VlbRATlNG SCREEN VS
DOUBLE DECK VIBRATING SCREEN VS
TRIPLE DLCK VIBRATING SCREEN VS
SEE ALSO SEPARATORS
VIBRATING SCREEN VS
VIBRATING CONVEYOR CO
ALSO SEE SEPARATOR
WASHERS
WASTE RECOVERY/TREATING UNITS
WATER CONDITIONING SYSTEM
WATER CONDITIONING/TREATING UNITS
WATER POLLUTION EQUIPMENT
HATER SOFTENING SYSTEM
WATER TREATMENT SYSTEMS
WEAK BASE-STRONG bASE ANION1C
WEIGHING SYSTEM
WEIGH SCALES
WETTED-WALL COLUMNS
WIPED FILM EVAPORATORS
WASHERS HC
SEE ALSO SCRUBBERS
SEE UNDER SPECIFIC ITEM
WATER TREATMENT SYSTEM WTS
ION EXCHANGER IE
PACKED COLUMN TW
PACKING TW
AIR CONDITIONING UNIT ACU
AIR DRYEH AD
WATER TREATMENT SYSTEMS WTS
SEE UNDER SPECIFIC ITEM
WATER TREATMENT SYSTEM WTS
ION EXCHANGER IE
PACKING TW
PACKED COLUMN TW
ALSO SEE PI^IP
DEMINERALIZING SYSTEM WTS
SOFTENING TREATMENT SYSTEM WTS
FILTERING TREATMENT WTS
PUMPING STATION WTS
WATER STILL WTS
STEAM BOILER WTS
PACKAGED BOILER UNIT WTS
FIELD ERECTED bOILtR UNIT WTS
COOLING TOWER SYSTEM WTS
SEE ALSO UNDER SPECIFIC ITEM
ION EXCHANGER IE
SCALE S
CONVEYOR CO
FEEDER FE
SCALES S
EVAPORATOR ,' E
PACKED COLUMN TW
WIPED FILM EVAPORATOR WFE
AGITATED THIN FILM EVAPORATOR WFE
AGITATED THIN FILM EVAPORATOR - PACK-
ED SYSTEM WFE
SEE ALSO EVAPORATORS' DRUM DRYERS'
FLAKERS
182
-------
COMMON EQUIPMENT XTLM
MODUL.E NAME
AIR COMPRESSOR
AIR COMPRESSOR
AIR CONDITIONING UNIT
AIR CONDITIONING UNIT
AIR DRYER
AGITATED OPEN TANK
AGITATED PRESSURE TANK
AERATION SYSTEM
BLENDER
BLENDER
CONDENSER
CONVEYOR
CRANE
APRON CONVEYOR
ROLLER CONVENOR
PNEUMATIC CONVEYING SYSTEM
BUCKET CONVEYOR
CENTRIFUGAL PUMP
CRUSHER
CRYSTALLIZER
CRYSTALLI2ER
CENTRIFUGE
CENTRIFUGE
CUTTER
DRYER
DRYER
DUST COLLECTOR
DRY CAUSTIC PEELER
DRUM DRYER
EVAPORATOR
EVAPORATOR
ELECTRODIALYSIS
ELECTRIC GENERATOR
ELECTRIC GENERATOR
EJECTOR
ELEVATOR
EQUALIZATION SYSTEM
EXTRACTOR
FILTER
FILTER
FEEDER
FEEDER
FEEDER
FLAKER
FLOATATION MACHINE
FAN
FREEZER
FURNACE
GEAR PUMP
HOT AIR BLANCHER
HEAT EXCHANGER
ELECTRICAL HEATER
HOIST
HORIZONTAL TANK
HEATING UNIT
INCINERATOR
IMPRESSED VOLTAGE SYSTEM
ION EXCHANGER
KNEADER
LAGOON SYSTEM
MILL
MILL
MIXER
MIXER
PUMP
PUMP
PACKAGING MACHINE
PRESS
REACTOR
ROTARY DRYER
REVERSE OSMOSIS SYSTEM
RAILROAD TANK CAR
REFRIGERATION UNIT
SUBMERGED COMBUSTION SYSTEM
SEDIMENTATION SYSTEM
STACK
THICKENER
TRICKLING FILTER
TRAY TOWER
COOLING TOWER
PACKED COLUMN
ULTRAFILTRATION SYSTEM
VACUUM PUMP
VIBRATING SCREEN
VERTICAL TANK
WATER TREATMENT SYSTEM
STEAM BOILER
WATER STILL
APPENDIX G
DATA SHEET INDEX
.
! DATA
DETERMINING ECONOMIC PARAMETER JSHEFT
: DESCRIPTION
INLLT CAPACITY
DRIVER POWER
CAPACITY
POWER
CAPACITY
CAPACITY
OVERALL CAPACITY
CAPACITY
DRIVER POWER
CAPACITY
WATER RATE
LENGTH
CAPACITY
LENGTH
LENGTH
OVt-KALL SYSTEM LENGTH
LtNGTH
FLOWRATE AND HEAD
FLOWRATE
FLOWRATE
LENGTH
DRIVER POWER
BOwL DIAMETER
DRIVER POWER
EVAPORATION RATE
HEAT TRANSFER SURFACE
INLET CAPACITY
PRODUCT FLOWRATE
HEAT TRANSFER SURFACE
CAPACITY
HEAT TRANSFER SURFACE
CAPACITY
CAPACITY
CAPACITY
FLOWRATE
LIFT
CAPACITY
CAPACITY
DIAMETER
FILTRATION AREA
FLOWRATE
SIZE
FLOWRATE
SUKFACE AREA
CAPACITY
FLOtfKATE
CAPACITY
HEAT TRANSFER DUTY
FLOWRATE
CAPACITY
HEAT TRANSFER AREA
CAPACITY
CAPACITY
TOTAL CAPACITY
CAPACITY
CAPACITY
TOTAL CAPACITY
RESIN VOLUME
CAPACITY
DESIGN FLOW
PRODUCT CAPACITY
DRIVER POWER
PRODUCT CAPACITY
DRIVER POWER
DRIVER POWER
FLOWRATE
BAGGING RATE
AREA
DIAMETER
HEAT TRANSFER AREA
FLOWRATE
CAPACITY
CAPACITY
CAPACITY
CAPACITY
LENGTH
DIAMETER
CAPACITY
DIAMETER AND NO. TRAYS
FLOWRATE
DIAMETER AND HEIGHT
CAPACITY
CAPACITY
AREA
CAPACITY
CAPACITY
CAPACITY
CAPACITY
: UNITS : NO.
CUBIC FEET PER MINUTE AC-1
tIRAKE HORSEPOWER AC-1
IONS HCU-1
HORSEPOWER ACU-1
CUBIC FEET PER MINUTE AD-t
GALLONS AOT-I
GALLONS /IPT-1
MILLIONS GALLONS/DAY AS-I
HORSEPOWER BL-t
CUBIC FEET RL-1
GALLONS PER MINUTE C-l
FtET CO-1
TONS CE-)
FEET co--?
FEET co--;
FEET CO-7
FEET CO-9
GALLONS/MINUTE - FEET CP-I
TONS PER DAY CR-1
TONS PER DAY CRY-1
FEET CRY-1
HORSEPOWER CT-1
INCHES CT-1
HORSEPOWER CU-1
POUNDS WATER PER HOUR D-l
SQUARE FEET D-l
CUBIC FEET PER MINUTE DC-1
TONS PER HOUR ncp-i
SQUARE FEET DD-1
GALLONS E-l
SQUARE FEET E-l
GALLONS PER MINUTE ED-1
KILLOWATTS EG-1
KILLOVOLT-AMPHERF.S EG-t
POUNDS AIR PER HOUR EJ-1
FEET EL-1
MILLIONS GALLONS/DAY ES-1
GALLONS PER MINUTE EX-1
INCHES F-1
SQUARE FEET F-1
CUBIC FEET PER HOUR FE-1
NUMBER FE-1
POUNDS PER HOUR FE-1
SQUARE FEET FL-1
CUBIC FEET FM-1
CUBIC FEET PER MINUTE FN-1
CUBIC FEET FR-1
MILLIONS BTU PER HOUR FU-l
GALLONS PER MINUTE GP-1
bTU PER HOUR HAB-1
SOUARE FEET HE-I
MLLOWATTS HE-3
TONS HO-1
GALLONS HT-1
MILLION BTU PER HOUR HU-I
POUNDS SOLIDS PER HOUR 1-1
GALLONS IVS-1
CUBIC FEET IE-1
GALLONS K-l
MILLIONS GALLONS/DAY LS-1
TONS PER DAY M-l
HORSEPOWER M-l
CUBIC FEET MX-1
HORSEPOWER MX-1
HORSEPOWER P-l
GALLONS PER MINUTE P-l
BAGS PER MINUTE PKG-1
SQUARE FEET P-l
FEET R-l
SQUARE FEET RD-I
GALLONS PER MIMUTE ROS-1
GALLONS RTC-1
TONS RU-t
MILLION BTU PER HOUR SCS-1
MILLION GALLONS/DAY SS-1
FEET STK-1
FEET T-l
GALLONS PER MINUTE TF-1
FEET TW-1
GALLONS PER MINUTE TW-3
FEET TW-5
GALLONS PER MINUTE US-1
CUBIC FEET PER MINUTE VP-1
SQUARE FEET VS-1
GALLONS VT-1
GALLONS PER MINUTE WTS-1
POUNDS STEAM PER HOUR WTS-3
GALLONS PER DAY WTS-5
183
»US GOVERNMENT PRINTING OFFICE. 1973-546-309/63
-------
SELECTED WATER
RESOURCES ABSTRACTS
INPUT TRANSACTION FORM
f. Rep/ tNo.
w
Capital and Operating Costs of Pollution Control
Equipment Modules, Data Manual (Volume II)
Herbert G. Blecker, Theodore W. Cadman
ICARUS Corporation
Silver Spring, MD
12. Sponsori
5,
e.
PfTfarmmf Oigitt!fstioa
Report Kir,
21AQJ
68-01-0717
13- Type{ ' Repor jnd
Period Covered
Environmental Protection Agency,
report number, EPA-R5-73-023b, July 1973.
This Data Manual presents, in convenient graphical and tabular form,
cost information for installed equipment item modules on separate data
sheets. Each data sheet conforms to a uniform style providing information
on the specific item and adjustments to atypical installation, construction,
or design. The methodology used in developing this data and the techniques
suggested for its use are described in detail in the companion User Guide.
rJe=cn;to«*Cost Analysis, *Costs, *Pollution Abatement, Cost Comparisons, Economics,
Annual Costs, Construction Costs, Operating Costs, Estimated Costs, Manuals,
*Engineers Estimates, *Data Collections
J$S S*etf*fty £*•*»».'
(R*t>t>rt)
SO, Security Class,
21. "tfo. ff -
Pages
22. Price
Send To:
WATER RESOURCES SCIENTIFIC INFORMATION CENTER
US DEPARTMENT OF THE INTERIOR
WASHINGTON. D C 2O24O
Fred H. Abel
Environmental Protection Agency
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