Appendix
A
Very
Small
Systems
Model
Capital
Cost
Breakdown
Summaries
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
June
2003
A­
1
Appendix
A
Contents
Exhibit
Name
Exhibit
Number
VSS
Document
Capital
Cost
Breakdown
for
Membrane
Processes
A1
VSS
Document
Capital
Cost
Breakdown
for
Ion
Exchange
Processes
A2
VSS
Document
Capital
Cost
Breakdown
for
Chlorination
A3
VSS
Document
Capital
Cost
Breakdown
for
Potassium
Permanganate
Feed
A4
Typical
VSS
Document
Capital
Cost
Breakdown
A5
Below
is
an
explanation
of
the
abbreviations
used
in
this
appendix:

p
­
The
cost
belongs
to
the
process
cost
category
of
capital
cost
breakdown
c
­
The
cost
belongs
to
the
construction
cost
category
of
the
capital
cost
breakdown
e
­
The
cost
belongs
to
the
engineering
cost
category
of
the
capital
cost
breakdown
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
A1
­
VSS
Document
Capital
Cost
Breakdown
for
Membrane
Processes
Component
Capital
Cost
Factor
Percent
of
Total
Capital
Cost
Capital
Cost
Breakdown
Category
Equipment
1.0000
56.97%
p
Installation
0.2500
14.24%
c
Sitework/
Interface
Piping
0.0750
4.27%
c
Standby
Power
0.0625
3.56%
c
OH&
P
0.1665
9.49%
e
Legal
&
Admin
0.0416
2.37%
e
Engineering
0.1596
9.09%
e
Contigencies
0.0000
0.00%
c
Total
1.7552
100.00%

Exhibit
A2
­
VSS
Document
Capital
Cost
Breakdown
for
Ion
Exchange
Processes
Component
Capital
Cost
Factor
Percent
of
Total
Capital
Cost
Capital
Cost
Breakdown
Category
Equipment
1.0000
54.78%
p
Installation
0.3000
16.43%
c
Sitework/
Interface
Piping
0.0780
4.27%
c
Standby
Power
0.0650
3.56%
c
OH&
P
0.1732
9.49%
e
Legal
&
Admin
0.0433
2.37%
e
Engineering
0.1659
9.09%
e
Contigencies
0.0000
0.00%
c
Total
1.8254
100.00%

A­
2
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
A3
­
VSS
Document
Capital
Cost
Breakdown
for
Chlorination
Component
Capital
Cost
Factor
Percent
of
Total
Capital
Cost
Capital
Cost
Breakdown
Category
Equipment
1.0000
61.93%
p
Installation
0.1500
9.29%
c
Sitework/
Interface
Piping
0.0690
4.27%
c
Standby
Power
0.0575
3.56%
c
OH&
P
0.1532
9.49%
e
Legal
&
Admin
0.0383
2.37%
e
Engineering
0.1468
9.09%
e
Contigencies
0.0000
0.00%
c
Total
1.6148
100.00%

Exhibit
A4
­
VSS
Document
Capital
Cost
Breakdown
for
Potassium
Permanganate
Feed
Component
Capital
Cost
Factor
Percent
of
Total
Capital
Cost
Capital
Cost
Breakdown
Category
Equipment
1.0000
64.74%
p
Installation
0.1000
6.47%
c
Sitework/
Interface
Piping
0.0660
4.27%
c
Standby
Power
0.0550
3.56%
c
OH&
P
0.1465
9.49%
e
Legal
&
Admin
0.0366
2.37%
e
Engineering
0.1404
9.09%
e
Contigencies
0.0000
0.00%
c
Total
1.5446
100.00%

A­
3
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
A5
­
Typical
VSS
Document
Capital
Cost
Breakdown
Component
Capital
Cost
Factor
Percent
of
Total
Capital
Cost
Capital
Cost
Breakdown
Category
Equipment
1.0000
54.78%
p
Installation
0.3000
16.43%
c
Sitework/
Interface
Piping
0.0780
4.27%
c
Standby
Power
0.0650
3.56%
c
OH&
P
0.1732
9.49%
e
Legal
&
Admin
0.0433
2.37%
e
Engineering
0.1659
9.09%
e
Contigencies
0.0000
0.00%
c
Total
1.8254
100.00%

A­
4
June
2003
Appendix
B
Water
Model
Capital
Cost
Breakdown
Summaries
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
June
2003
B­
1
Appendix
B
Contents
Exhibit
Name
Exhibit
Number
Base
Costs
Obtained
from
the
Water
Model
for
Activated
Alumina
Exhibit
B1.1
Water
Model
Base
Construction
Cost
Analysis
for
Activated
Alumina
Exhibit
B1.2
Base
Costs
Obtained
from
the
Water
Model
for
Anion
Exchange
Exhibit
B2.1
Water
Model
Base
Construction
Cost
Analysis
for
Anion
Exchange
Exhibit
B2.2
Base
Costs
Obtained
from
the
Water
Model
for
Basic
Chemical
Feed
Exhibit
B3.1
Water
Model
Base
Construction
Cost
Analysis
for
Basic
Chemical
Feed
Exhibit
B3.2
Base
Costs
Obtained
from
the
Water
Model
for
Chlorination
Exhibit
B4.1
Water
Model
Base
Construction
Cost
Analysis
for
Chlorination
Exhibit
B4.2
Base
Costs
Obtained
from
the
Water
Model
for
Underground
Clearwell
Storage
Exhibit
B5.1
Water
Model
Base
Construction
Cost
Analysis
for
Underground
Clearwell
Storage
Exhibit
B5.2
Base
Costs
Obtained
from
the
Water
Model
for
Package
Conventional
Treatment
Exhibit
B6.1
Water
Model
Base
Construction
Cost
Analysis
for
Package
Conventional
Treatment
Exhibit
B6.2
Base
Costs
Obtained
from
the
Water
Model
for
Ferric
Chloride
Feed
Exhibit
B7.1
Water
Model
Base
Construction
Cost
Analysis
for
Ferric
Chloride
Feed
Exhibit
B7.2
Base
Costs
Obtained
from
the
Water
Model
for
Package
Lime
Softening
Exhibit
B8.1
Water
Model
Base
Construction
Cost
Analysis
for
Package
Lime
Softening
Exhibit
B8.2
Base
Costs
Obtained
from
the
Water
Model
for
Permanganate
Feed
Exhibit
B9.1
Water
Model
Base
Construction
Cost
Analysis
for
Permanganate
Feed
Exhibit
B9.2
Base
Costs
Obtained
from
the
Water
Model
for
Polymer
Feed
Exhibit
B10.1
Water
Model
Base
Construction
Cost
Analysis
for
Polymer
Feed
Exhibit
B10.2
Base
Costs
Obtained
from
the
Water
Model
for
Raw
Water
Pumping
Exhibit
B11.1
Water
Model
Base
Construction
Cost
Analysis
for
Raw
Water
Pumping
Exhibit
B11.2
Base
Costs
Obtained
from
the
Water
Model
for
Package
Reverse
Osmosis
Exhibit
B12.1
Water
Model
Base
Construction
Cost
Analysis
for
Package
Reverse
Osmosis
Exhibit
B12.2
Base
Costs
Obtained
from
the
Water
Model
for
Sodium
Hydroxide
Feed
Exhibit
B13.1
Water
Model
Base
Construction
Cost
Analysis
for
Sodium
Hydroxide
Feed
Exhibit
B13.2
Base
Costs
Obtained
from
the
Water
Model
for
Package
Ultrafiltration
Exhibit
B14.1
Water
Model
Base
Construction
Cost
Analysis
for
Package
Ultrafiltration
Exhibit
B14.2
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
June
2003
B­
2
Below
is
an
explanation
of
the
abbreviations
used
in
this
appendix:

p
­
The
cost
belongs
to
the
process
cost
category
of
capital
cost
breakdown
c
­
The
cost
belongs
to
the
construction
cost
category
of
the
capital
cost
breakdown
e
­
The
cost
belongs
to
the
engineering
cost
category
of
the
capital
cost
breakdown
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B1.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Activated
Alumina
Contactor
Volume
(
ft3)
32
71
126
283
385
502
754
Excavation
&
Sitework
$
4,700
$
4,700
$
4,700
$
4,700
$
4,700
$
4,700
$
4,700
c
Manufactured
Equipment
$
12,800
$
23,900
$
39,100
$
50,600
$
64,500
$
72,900
$
101,000
p
Activated
Alumina
$
1,400
$
3,100
$
5,400
$
11,900
$
15,400
$
19,600
$
29,400
p
Concrete
$
400
$
1,200
$
1,800
$
2,000
$
2,500
$
3,200
$
4,100
p
Labor
$
1,200
$
1,500
$
2,000
$
2,800
$
3,300
$
3,400
$
4,200
c
Pipes
and
Valves
$
5,200
$
6,500
$
6,500
$
8,400
$
12,800
$
13,300
$
20,100
p
Electrical
$
6,400
$
6,400
$
6,400
$
8,000
$
8,000
$
8,500
$
9,600
p
Housing
$
8,700
$
14,400
$
16,900
$
17,900
$
24,800
$
34,400
$
43,900
p
Subtotal
$
40,800
$
61,700
$
82,800
$
106,300
$
136,000
$
160,000
$
217,000
Contingencies
$
6,100
$
9,300
$
12,400
$
15,900
$
20,400
$
24,000
$
32,600
c
Total
$
46,900
$
71,000
$
95,200
$
122,200
$
156,400
$
184,000
$
249,600
Exhibit
B1.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Activated
Alumina
Contactor
Volume
(
ft3)
32
71
126
283
385
502
754
Excavation
&
Sitework
10.02%
6.62%
4.94%
3.85%
3.01%
2.55%
1.88%
4.70%
Manufactured
Equipment
27.29%
33.66%
41.07%
41.41%
41.24%
39.62%
40.46%
37.82%
Activated
Alumina
2.99%
4.37%
5.67%
9.74%
9.85%
10.65%
11.78%
7.86%
Concrete
0.85%
1.69%
1.89%
1.64%
1.60%
1.74%
1.64%
1.58%
Labor
2.56%
2.11%
2.10%
2.29%
2.11%
1.85%
1.68%
2.10%
Pipes
and
Valves
11.09%
9.15%
6.83%
6.87%
8.18%
7.23%
8.05%
8.20%
Electrical
13.65%
9.01%
6.72%
6.55%
5.12%
4.62%
3.85%
7.07%
Housing
18.55%
20.28%
17.75%
14.65%
15.86%
18.70%
17.59%
17.62%
Contingencies
13.01%
13.10%
13.03%
13.01%
13.04%
13.04%
13.06%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
3
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B2.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Anion
Exchange
Resin
Volume
(
ft3)
4
17
54
188
280
520
Excavation
&
Sitework
$
2,100
$
2,100
$
4,400
$
4,400
$
4,400
$
5,300
c
Manufactured
Equipment
$
3,100
$
8,600
$
23,100
$
64,100
$
96,800
$
164,800
p
Concrete
$
300
$
400
$
5,500
$
5,800
$
6,000
$
8,400
p
Steel
$
0
$
0
$
7,800
$
7,800
$
7,800
$
10,900
p
Labor
$
400
$
1,100
$
12,100
$
12,800
$
12,900
$
17,200
c
Pipes
and
Valves
$
800
$
800
$
1,000
$
2,600
$
2,600
$
3,100
p
Electrical
$
3,100
$
3,100
$
3,100
$
3,100
$
3,100
$
3,100
p
Housing
$
5,600
$
9,600
$
11,100
$
16,600
$
19,200
$
25,000
p
Subtotal
$
15,400
$
25,700
$
68,100
$
117,200
$
152,800
$
237,800
Contingencies
$
2,300
$
3,900
$
10,200
$
17,600
$
22,900
$
35,700
c
Total
$
17,700
$
29,600
$
78,300
$
134,800
$
175,700
$
273,500
Exhibit
B2.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Anion
Exchange
Resin
Volume
(
ft3)
4
17
54
188
280
520
Excavation
&
Sitework
11.86%
7.09%
5.62%
3.26%
2.50%
1.94%
5.38%
Manufactured
Equipment
17.51%
29.05%
29.50%
47.55%
55.09%
60.26%
39.83%
Concrete
1.69%
1.35%
7.02%
4.30%
3.41%
3.07%
3.48%
Steel
0.00%
0.00%
9.96%
5.79%
4.44%
3.99%
4.03%
Labor
2.26%
3.72%
15.45%
9.50%
7.34%
6.29%
7.43%
Pipes
and
Valves
4.52%
2.70%
1.28%
1.93%
1.48%
1.13%
2.17%
Electrical
17.51%
10.47%
3.96%
2.30%
1.76%
1.13%
6.19%
Housing
31.64%
32.43%
14.18%
12.31%
10.93%
9.14%
18.44%
Contingencies
12.99%
13.18%
13.03%
13.06%
13.03%
13.05%
13.06%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
4
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B3.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Basic
Chemical
Feed
Maximum
Feed
Rate
(
lb/
day)
0.1­
10
25
50
100
250
500
1000
Dissolving
Tank
$
290
$
430
$
640
$
910
$
1,830
$
2,200
$
4,400
p
Mixer
$
180
$
200
$
200
$
240
$
410
$
620
$
620
p
Metering
Pump
$
430
$
700
$
750
$
1,230
$
1,600
$
1,670
$
1,820
p
Pipes
and
Valves
$
180
$
180
$
220
$
220
$
280
$
280
$
420
p
Labor
$
180
$
180
$
240
$
260
$
300
$
330
$
400
c
Electrical
$
80
$
100
$
150
$
200
$
250
$
300
$
400
p
Subtotal
$
1,340
$
1,790
$
2,200
$
3,060
$
4,670
$
5,400
$
8,060
Contingencies
$
200
$
270
$
330
$
460
$
700
$
810
$
1,210
c
Total
$
1,540
$
2,060
$
2,530
$
3,520
$
5,370
$
6,210
$
9,270
Exhibit
B3.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Basic
Chemical
Feed
Maximum
Feed
Rate
(
lb/
day)
0.1­
10
25
50
100
250
500
1000
Dissolving
Tank
18.83%
20.87%
25.30%
25.85%
34.08%
35.43%
47.46%
29.69%
Mixer
11.69%
9.71%
7.91%
6.82%
7.64%
9.98%
6.69%
8.63%
Metering
Pump
27.92%
33.98%
29.64%
34.94%
29.80%
26.89%
19.63%
28.97%
Pipes
and
Valves
11.69%
8.74%
8.70%
6.25%
5.21%
4.51%
4.53%
7.09%
Labor
11.69%
8.74%
9.49%
7.39%
5.59%
5.31%
4.31%
7.50%
Electrical
5.19%
4.85%
5.93%
5.68%
4.66%
4.83%
4.31%
5.07%
Contingencies
12.99%
13.11%
13.04%
13.07%
13.04%
13.04%
13.05%
13.05%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
5
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B4.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Chlorination
Excavation
&
Sitework
$
1,200
c
Manufactured
Equipment
$
2,700
p
Concrete
$
300
p
Labor
$
400
c
Pipes
and
Valves
$
500
p
Electrical
$
2,200
p
Housing
$
7,800
p
Subtotal
$
15,100
Contingencies
$
2,300
c
Total
$
17,400
Exhibit
B4.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Chlorination
Excavation
&
Sitework
6.90%
6.90%
Manufactured
Equipment
15.52%
15.52%
Concrete
1.72%
1.72%
Labor
2.30%
2.30%
Pipes
and
Valves
2.87%
2.87%
Electrical
12.64%
12.64%
Housing
44.83%
44.83%
Contingencies
13.22%
13.22%
Total
100.00%
100.00%
Cost
Component
Cost
Capital
Cost
Category
Cost
Component
Cost
Average
Percent
B­
6
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B5.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Underground
Clearwell
Storage
Design
Capacity
(
gpd)
5,000
10,000
50,000
100,000
500,000
Excavation
&
Sitework
$
3,300
$
5,700
$
16,500
$
25,300
$
75,400
c
Concrete
$
9,800
$
16,500
$
37,000
$
64,000
$
216,400
p
Steel
$
300
$
400
$
500
$
500
$
600
p
Electrical
$
2,600
$
2,600
$
2,600
$
2,600
$
2,600
p
Subtotal
$
16,000
$
25,200
$
56,600
$
92,400
$
295,000
Contingencies
$
2,400
$
3,800
$
8,500
$
13,900
$
44,300
c
Total
$
18,400
$
29,000
$
65,100
$
106,300
$
339,300
Exhibit
B5.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Underground
Clearwell
Storage
Design
Capacity
(
gpd)
5,000
10,000
50,000
100,000
500,000
Excavation
&
Sitework
17.93%
19.66%
25.35%
23.80%
22.22%
21.79%
Concrete
53.26%
56.90%
56.84%
60.21%
63.78%
58.20%
Steel
1.63%
1.38%
0.77%
0.47%
0.18%
0.88%
Electrical
14.13%
8.97%
3.99%
2.45%
0.77%
6.06%
Contingencies
13.04%
13.10%
13.06%
13.08%
13.06%
13.07%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
7
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B6.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Package
Conventional
Treatment
Filter
Area
(
ft2)
2
12
20
40
112
150
Excavation
&
Sitework
$
3,500
$
3,500
$
4,700
$
5,800
$
7,000
$
9,300
c
Manufactured
Equipment
$
31,000
$
44,900
$
53,500
$
111,300
$
176,600
$
190,500
p
Concrete
$
1,000
$
1,000
$
1,500
$
4,500
$
5,700
$
6,800
p
Labor
$
9,900
$
14,700
$
17,500
$
36,400
$
57,800
$
62,400
c
Pipes
and
Valves
$
4,200
$
8,300
$
10,400
$
20,900
$
29,200
$
41,700
p
Electrical
$
3,200
$
4,500
$
5,300
$
11,100
$
17,600
$
19,000
p
Housing
$
18,600
$
18,600
$
23,400
$
45,000
$
47,500
$
52,500
p
Subtotal
$
71,400
$
95,500
$
116,300
$
235,000
$
341,400
$
382,200
Contingencies
$
10,700
$
14,300
$
17,400
$
35,300
$
51,200
$
57,300
c
Total
$
82,100
$
109,800
$
133,700
$
270,300
$
392,600
$
439,500
Exhibit
B6.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Package
Conventional
Treatment
Filter
Area
(
ft2)
2
12
20
40
112
150
Excavation
&
Sitework
4.26%
3.19%
3.52%
2.15%
1.78%
2.12%
2.84%
Manufactured
Equipment
37.76%
40.89%
40.01%
41.18%
44.98%
43.34%
41.36%
Concrete
1.22%
0.91%
1.12%
1.66%
1.45%
1.55%
1.32%
Labor
12.06%
13.39%
13.09%
13.47%
14.72%
14.20%
13.49%
Pipes
and
Valves
5.12%
7.56%
7.78%
7.73%
7.44%
9.49%
7.52%
Electrical
3.90%
4.10%
3.96%
4.11%
4.48%
4.32%
4.15%
Housing
22.66%
16.94%
17.50%
16.65%
12.10%
11.95%
16.30%
Contingencies
13.03%
13.02%
13.01%
13.06%
13.04%
13.04%
13.03%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
8
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B7.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Ferric
Chloride
Feed
Maximum
Feed
Rate
(
lb/
day)
1
10
25
50
100
250
750
Storage
Tank
$
0
$
0
$
0
$
0
$
360
$
780
$
2,040
p
Wooden
Stairway
$
0
$
0
$
0
$
0
$
0
$
300
$
300
p
Metering
Pump
$
390
$
390
$
390
$
390
$
390
$
1,090
$
1,100
p
Pipes
and
Valves
$
180
$
180
$
180
$
180
$
220
$
280
$
280
p
Labor
$
120
$
120
$
130
$
130
$
210
$
360
$
410
c
Electrical
$
80
$
80
$
80
$
80
$
100
$
120
$
120
p
Subtotal
$
770
$
770
$
780
$
780
$
1,280
$
2,930
$
4,250
Contingencies
$
120
$
120
$
120
$
120
$
190
$
440
$
640
c
Total
$
890
$
890
$
900
$
900
$
1,470
$
3,370
$
4,890
Exhibit
B7.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Ferric
Chloride
Feed
Maximum
Feed
Rate
(
lb/
day)
1
10
25
50
100
250
750
Storage
Tank
0.00%
0.00%
0.00%
0.00%
24.49%
23.15%
41.72%
12.76%
Wooden
Stairway
0.00%
0.00%
0.00%
0.00%
0.00%
8.90%
6.13%
2.15%
Metering
Pump
43.82%
43.82%
43.33%
43.33%
26.53%
32.34%
22.49%
36.53%
Pipes
and
Valves
20.22%
20.22%
20.00%
20.00%
14.97%
8.31%
5.73%
15.64%
Labor
13.48%
13.48%
14.44%
14.44%
14.29%
10.68%
8.38%
12.74%
Electrical
8.99%
8.99%
8.89%
8.89%
6.80%
3.56%
2.45%
6.94%
Contingencies
13.48%
13.48%
13.33%
13.33%
12.93%
13.06%
13.09%
13.24%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
9
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B8.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Package
Lime
Softening
Design
Capacity
(
gpd)
15,000
150,000
430,000
750,000
1,000,000
Excavation
&
Sitework
$
3,500
$
5,800
$
6,700
$
8,400
$
9,800
c
Manufactured
Equipment
$
33,200
$
49,800
$
66,300
$
86,200
$
103,800
p
Concrete
$
1,100
$
2,500
$
3,200
$
5,900
$
7,000
p
Labor
$
14,000
$
18,200
$
28,000
$
36,400
$
43,800
c
Pipes
and
Valves
$
5,200
$
10,400
$
14,100
$
16,700
$
45,900
p
Electrical
$
8,500
$
12,200
$
17,000
$
18,900
$
26,700
p
Housing
$
8,800
$
16,400
$
19,800
$
30,000
$
33,000
p
Subtotal
$
74,300
$
115,300
$
155,100
$
202,500
$
270,000
Contingencies
$
11,100
$
17,300
$
23,300
$
30,400
$
40,500
c
Total
$
85,400
$
132,600
$
178,400
$
232,900
$
310,500
Exhibit
B8.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Package
Lime
Softening
Design
Capacity
(
gpd)
15,000
150,000
430,000
750,000
1,000,000
Excavation
&
Sitework
4.10%
4.37%
3.76%
3.61%
3.16%
3.80%
Manufactured
Equipment
38.88%
37.56%
37.16%
37.01%
33.43%
36.81%
Concrete
1.29%
1.89%
1.79%
2.53%
2.25%
1.95%
Labor
16.39%
13.73%
15.70%
15.63%
14.11%
15.11%
Pipes
and
Valves
6.09%
7.84%
7.90%
7.17%
14.78%
8.76%
Electrical
9.95%
9.20%
9.53%
8.12%
8.60%
9.08%
Housing
10.30%
12.37%
11.10%
12.88%
10.63%
11.46%
Contingencies
13.00%
13.05%
13.06%
13.05%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
10
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B9.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Permanganate
Feed
Maximum
Feed
Rate
(
lb/
day)
0.5­
5
12.5
25
50
125
250
Dissolving
Tank
$
290
$
430
$
640
$
910
$
1,830
$
2,200
p
Mixer
$
180
$
200
$
200
$
240
$
410
$
620
p
Metering
Pump
$
430
$
700
$
750
$
1,230
$
1,600
$
1,670
p
Pipes
and
Valves
$
180
$
180
$
220
$
220
$
280
$
280
p
Labor
$
180
$
180
$
240
$
260
$
300
$
330
c
Electrical
$
80
$
100
$
150
$
200
$
250
$
300
p
Subtotal
$
1,340
$
1,790
$
2,200
$
3,060
$
4,670
$
5,400
Contingencies
$
200
$
270
$
330
$
460
$
700
$
810
c
Total
$
1,540
$
2,060
$
2,530
$
3,520
$
5,370
$
6,210
Exhibit
B9.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Permanganate
Feed
Maximum
Feed
Rate
(
lb/
day)
0.5­
5
12.5
25
50
125
250
Excavation
&
Sitework
18.83%
20.87%
25.30%
25.85%
34.08%
35.43%
26.73%
Manufactured
Equipment
11.69%
9.71%
7.91%
6.82%
7.64%
9.98%
8.96%
Concrete
27.92%
33.98%
29.64%
34.94%
29.80%
26.89%
30.53%
Labor
11.69%
8.74%
8.70%
6.25%
5.21%
4.51%
7.52%
Pipes
and
Valves
11.69%
8.74%
9.49%
7.39%
5.59%
5.31%
8.03%
Electrical
5.19%
4.85%
5.93%
5.68%
4.66%
4.83%
5.19%
Contingencies
12.99%
13.11%
13.04%
13.07%
13.04%
13.04%
13.05%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
11
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B10.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Polymer
Feed
Maximum
Feed
Rate
(
lb/
day)
0.6
1
2.1
4.2
10.4
Mixing
Tank
$
290
$
430
$
640
$
910
$
1,830
p
Mixer
$
850
$
850
$
200
$
1,050
$
1,050
p
Metering
Pump
$
640
$
700
$
750
$
1,230
$
1,600
p
Pipes
and
Valves
$
180
$
180
$
220
$
220
$
280
p
Labor
$
180
$
180
$
240
$
260
$
300
c
Electrical
$
80
$
100
$
150
$
200
$
250
p
Subtotal
$
2,220
$
2,440
$
2,200
$
3,870
$
5,310
Contingencies
$
330
$
370
$
330
$
580
$
800
c
Total
$
2,550
$
2,810
$
2,530
$
4,450
$
6,110
Exhibit
B10.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Polymer
Feed
Maximum
Feed
Rate
(
lb/
day)
0.6
1
2.1
4.2
10.4
Mixing
Tank
11.37%
15.30%
25.30%
20.45%
29.95%
20.47%
Mixer
33.33%
30.25%
7.91%
23.60%
17.18%
22.45%
Metering
Pump
25.10%
24.91%
29.64%
27.64%
26.19%
26.70%
Pipes
and
Valves
7.06%
6.41%
8.70%
4.94%
4.58%
6.34%
Labor
7.06%
6.41%
9.49%
5.84%
4.91%
6.74%
Electrical
3.14%
3.56%
5.93%
4.49%
4.09%
4.24%
Contingencies
12.94%
13.17%
13.04%
13.03%
13.09%
13.06%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
12
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B11.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Raw
Water
Pumping
Design
Capacity
(
gpd)
28,800
144,000
504,000
720,000
1,008,000
Excavation
&
Sitework
$
11,700
$
11,700
$
12,300
$
12,300
$
12,800
c
Manufactured
Equipment
$
6,600
$
7,800
$
11,800
$
12,600
$
16,500
p
Concrete
$
500
$
500
$
1,100
$
1,100
$
1,500
p
Labor
$
3,700
$
3,800
$
5,800
$
6,200
$
8,500
c
Pipes
and
Valves
$
1,500
$
1,800
$
2,700
$
3,600
$
4,500
p
Electrical
$
800
$
800
$
1,400
$
1,600
$
2,100
p
Subtotal
$
24,800
$
26,400
$
35,100
$
37,400
$
45,900
Contingencies
$
3,700
$
4,000
$
5,300
$
5,600
$
6,900
c
Total
$
28,500
$
30,400
$
40,400
$
43,000
$
52,800
Exhibit
B11.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Raw
Water
Pumping
Design
Capacity
(
gpd)
28,800
144,000
504,000
720,000
1,008,000
Excavation
&
Sitework
41.05%
38.49%
30.45%
28.60%
24.24%
32.57%
Manufactured
Equipment
23.16%
25.66%
29.21%
29.30%
31.25%
27.72%
Concrete
1.75%
1.64%
2.72%
2.56%
2.84%
2.30%
Labor
12.98%
12.50%
14.36%
14.42%
16.10%
14.07%
Pipes
and
Valves
5.26%
5.92%
6.68%
8.37%
8.52%
6.95%
Electrical
2.81%
2.63%
3.47%
3.72%
3.98%
3.32%
Contingencies
12.98%
13.16%
13.12%
13.02%
13.07%
13.07%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
13
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B12.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Package
Reverse
Osmosis
Plant
Capacity
(
gpd)
2,500
10,000
50,000
100,000
500,000
1,000,000
Manufactured
Equipment
$
20,300
$
30,000
$
69,600
$
123,000
$
454,800
$
877,400
p
Labor
$
800
$
1,200
$
1,500
$
2,800
$
7,500
$
14,600
c
Electrical
$
3,200
$
4,600
$
10,700
$
18,700
$
45,900
$
62,100
p
Housing
$
11,900
$
13,900
$
16,400
$
18,500
$
38,400
$
52,500
p
Subtotal
$
36,200
$
49,700
$
98,200
$
163,000
$
546,600
$
1,006,600
Contingencies
$
5,400
$
7,500
$
14,700
$
24,500
$
82,000
$
151,000
c
Total
$
41,600
$
57,200
$
112,900
$
187,500
$
628,600
$
1,157,600
Exhibit
B12.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Package
Reverse
Osmosis
Plant
Capacity
(
gpd)
2,500
10,000
50,000
100,000
500,000
1,000,000
Manufactured
Equipment
48.80%
52.45%
61.65%
65.60%
72.35%
75.79%
62.77%
Labor
1.92%
2.10%
1.33%
1.49%
1.19%
1.26%
1.55%
Electrical
7.69%
8.04%
9.48%
9.97%
7.30%
5.36%
7.98%
Housing
28.61%
24.30%
14.53%
9.87%
6.11%
4.54%
14.66%
Contingencies
12.98%
13.11%
13.02%
13.07%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
14
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B13.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Sodium
Hydroxide
Feed
Maximum
Feed
Rate
(
lb/
day)
0.8
4
8
42
83
417
834
Storage
and
Feed
Tanks
$
60
$
60
$
90
$
970
$
2,040
$
3,560
$
6,940
p
Heating
and
Insulation
$
0
$
0
$
0
$
200
$
410
$
950
$
1,620
p
Mixer
$
0
$
0
$
0
$
180
$
240
$
620
$
640
p
Stairway
$
0
$
0
$
0
$
0
$
0
$
300
$
600
p
Man.
Transfer
Pump
$
100
$
100
$
100
$
0
$
0
$
0
$
0
p
Pipes
and
Valves
$
310
$
310
$
310
$
470
$
470
$
530
$
790
p
Metering
Pump
$
390
$
390
$
390
$
390
$
410
$
1,090
$
1,100
p
Containment
Wall
$
120
$
120
$
150
$
270
$
400
$
600
$
880
p
Labor
$
280
$
280
$
280
$
420
$
480
$
650
$
860
c
Electrical
$
80
$
80
$
80
$
100
$
100
$
120
$
120
p
Subtotal
$
1,340
$
1,340
$
1,400
$
3,000
$
4,550
$
8,420
$
13,550
Contingencies
$
200
$
200
$
210
$
450
$
680
$
1,260
$
2,030
c
Total
$
1,540
$
1,540
$
1,610
$
3,450
$
5,230
$
9,680
$
15,580
Exhibit
B13.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Sodium
Hydroxide
Feed
Maximum
Feed
Rate
(
lb/
day)
0.8
4
8
42
83
417
834
Storage
and
Feed
Tanks
3.90%
3.90%
5.59%
28.12%
39.01%
36.78%
44.54%
23.12%
Heating
and
Insulation
0.00%
0.00%
0.00%
5.80%
7.84%
9.81%
10.40%
4.84%
Mixer
0.00%
0.00%
0.00%
5.22%
4.59%
6.40%
4.11%
2.90%
Stairway
0.00%
0.00%
0.00%
0.00%
0.00%
3.10%
3.85%
0.99%
Man.
Transfer
Pump
6.49%
6.49%
6.21%
0.00%
0.00%
0.00%
0.00%
2.74%
Pipes
and
Valves
20.13%
20.13%
19.25%
13.62%
8.99%
5.48%
5.07%
13.24%
Metering
Pump
25.32%
25.32%
24.22%
11.30%
7.84%
11.26%
7.06%
16.05%
Containment
Wall
7.79%
7.79%
9.32%
7.83%
7.65%
6.20%
5.65%
7.46%
Labor
18.18%
18.18%
17.39%
12.17%
9.18%
6.71%
5.52%
12.48%
Electrical
5.19%
5.19%
4.97%
2.90%
1.91%
1.24%
0.77%
3.17%
Contingencies
12.99%
12.99%
13.04%
13.04%
13.00%
13.02%
13.03%
13.02%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
15
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Exhibit
B14.1
­
Base
Costs
Obtained
from
the
Water
Model
for
Package
Ultrafiltration
Membrane
Area
(
ft2)
30
424
1,431
3,604
7,155
14,310
Excavation
&
Sitework
$
1,300
$
2,400
$
4,100
$
5,700
$
10,200
$
14,900
c
Manufactured
Equipment
$
5,500
$
25,300
$
65,600
$
129,800
$
23,900
$
415,100
p
Concrete
$
1,800
$
3,700
$
5,800
$
10,200
$
16,700
$
28,800
p
Labor
$
1,100
$
5,200
$
13,500
$
26,900
$
49,500
$
85,900
c
Pipes
and
Valves
$
500
$
1,100
$
2,200
$
3,800
$
4,500
$
6,200
p
Electrical
$
1,500
$
5,600
$
13,300
$
25,800
$
48,100
$
85,300
p
Housing
$
7,800
$
14,600
$
21,700
$
29,000
$
40,800
$
56,000
p
Subtotal
$
19,500
$
57,900
$
126,200
$
231,200
$
193,700
$
692,200
Contingencies
$
2,900
$
8,700
$
18,900
$
34,700
$
29,100
$
103,800
c
Total
$
22,400
$
66,600
$
145,100
$
265,900
$
222,800
$
796,000
Exhibit
B14.2
­
Water
Model
Base
Construction
Cost
Analysis
for
Package
Ultrafiltration
Membrane
Area
(
ft2)
30
424
1,431
3,604
7,155
14,310
Excavation
&
Sitework
5.80%
3.60%
2.83%
2.14%
4.58%
1.87%
3.47%
Manufactured
Equipment
24.55%
37.99%
45.21%
48.82%
10.73%
52.15%
36.57%
Concrete
8.04%
5.56%
4.00%
3.84%
7.50%
3.62%
5.42%
Labor
4.91%
7.81%
9.30%
10.12%
22.22%
10.79%
10.86%
Pipes
and
Valves
2.23%
1.65%
1.52%
1.43%
2.02%
0.78%
1.60%
Electrical
6.70%
8.41%
9.17%
9.70%
21.59%
10.72%
11.05%
Housing
34.82%
21.92%
14.96%
10.91%
18.31%
7.04%
17.99%
Contingencies
12.95%
13.06%
13.03%
13.05%
13.06%
13.04%
13.03%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
B­
16
June
2003
Appendix
C
W/
W
Cost
Model
Capital
Cost
Breakdown
Summaries
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
June
2003
C­
1
Appendix
C
Contents
Exhibit
Name
Exhibit
Number
Base
Costs
Obtained
from
the
WATER
Model
for
Activated
Alumina
C1.1
WATER
Model
Base
Construction
Cost
Analysis
for
Activated
Alumina
C1.2
Base
Costs
Obtained
from
the
WATER
Model
for
Ammonia
Feed
Systems
C2.1
WATER
Model
Base
Construction
Cost
Analysis
for
Ammonia
Feed
Systems
C2.2
Base
Costs
Obtained
from
the
WATER
Model
for
Backwash
Water
Pumping
C3.1
WATER
Model
Base
Construction
Cost
Analysis
for
Backwash
Water
Pumping
C3.2
Base
Costs
Obtained
from
the
WATER
Model
for
Chemical
Sludge
Pumping
C4.1
WATER
Model
Base
Construction
Cost
Analysis
for
Chemical
Sludge
Pumping
C4.2
Base
Costs
Obtained
from
the
WATER
Model
for
Chlorination
C5.1
WATER
Model
Base
Construction
Cost
Analysis
for
Chlorination
C5.2
Base
Costs
Obtained
from
the
WATER
Model
for
Circular
Clarifiers
C6.1
WATER
Model
Base
Construction
Cost
Analysis
for
Circular
Clarifiers
C6.2
Base
Costs
Obtained
from
the
WATER
Model
for
Clearwell
Storage
C7.1
WATER
Model
Base
Construction
Cost
Analysis
for
Clearwell
Storage
C7.2
Base
Costs
Obtained
from
the
WATER
Model
for
Ferric
Chloride
Feed
Systems
C8.1
WATER
Model
Base
Construction
Cost
Analysis
for
Ferric
Chloride
Feed
Systems
C8.2
Base
Costs
Obtained
from
the
WATER
Model
for
Finished
Water
Pumping
C9.1
WATER
Model
Base
Construction
Cost
Analysis
for
Finished
Water
Pumping
C9.2
Base
Costs
Obtained
from
the
WATER
Model
for
Gravity
Filtration
C10.1
WATER
Model
Base
Construction
Cost
Analysis
for
Gravity
Filtration
C10.2
Base
Costs
Obtained
from
the
WATER
Model
for
Horizontal
Paddle,
G=
50
C11.1
WATER
Model
Base
Construction
Cost
Analysis
for
Horizontal
Paddle,
G=
50
C11.2
Base
Costs
Obtained
from
the
WATER
Model
for
Horizontal
Paddle,
G=
80
C12.1
WATER
Model
Base
Construction
Cost
Analysis
for
Horizontal
Paddle,
G=
80
C12.2
Base
Costs
Obtained
from
the
WATER
Model
for
Hydraulic
Surface
Wash
C13.1
WATER
Model
Base
Construction
Cost
Analysis
for
Hydraulic
Surface
Wash
C13.2
Base
Costs
Obtained
from
the
WATER
Model
for
In­
Plant
Pumping
C14.1
WATER
Model
Base
Construction
Cost
Analysis
for
In­
Plant
Pumping
C14.2
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
June
2003
C­
2
Exhibit
Name
Exhibit
Number
Base
Costs
Obtained
from
the
WATER
Model
for
Ion
Exchange
C15.1
WATER
Model
Base
Construction
Cost
Analysis
for
Ion
Exchange
C15.2
Base
Costs
Obtained
from
the
WATER
Model
for
Lime
Feed
with
Recalcination
C16.1
WATER
Model
Base
Construction
Cost
Analysis
for
Lime
Feed
with
Recalcination
C16.2
Base
Costs
Obtained
from
the
WATER
Model
for
Permanganate
Feed
Systems
C17.1
WATER
Model
Base
Construction
Cost
Analysis
for
Permanganate
Feed
Systems
C17.2
Base
Costs
Obtained
from
the
WATER
Model
for
Polymer
Feed
Systems
C18.1
WATER
Model
Base
Construction
Cost
Analysis
for
Polymer
Feed
Systems
C18.2
Base
Costs
Obtained
from
the
WATER
Model
for
Rapid
Mix,
G=
900
C19.1
WATER
Model
Base
Construction
Cost
Analysis
for
Rapid
Mix,
G=
900
C19.2
Base
Costs
Obtained
from
the
WATER
Model
for
Recarbonation,
Liquid
Carbon
Dioxide
C20.1
WATER
Model
Base
Construction
Cost
Analysis
for
Recarbonation,
Liquid
Carbon
Dioxide
C20.2
Base
Costs
Obtained
from
the
WATER
Model
for
Recarbonation
Basins
C21.1
WATER
Model
Base
Construction
Cost
Analysis
for
Recarbonation
Basins
C21.2
Base
Costs
Obtained
from
the
WATER
Model
for
Rectangular
Clarifiers
C22.1
WATER
Model
Base
Construction
Cost
Analysis
for
Rectangular
Clarifiers
C22.2
Base
Costs
Obtained
from
the
WATER
Model
for
Reverse
Osmosis
C23.1
WATER
Model
Base
Construction
Cost
Analysis
for
Reverse
Osmosis
C23.2
Base
Costs
Obtained
from
the
WATER
Model
for
Sodium
Hydroxide
Feed
Systems
C24.1
WATER
Model
Base
Construction
Cost
Analysis
for
Sodium
Hydroxide
Feed
Systems
C24.2
Base
Costs
Obtained
from
the
WATER
Model
for
Sulfuric
Acid
Feed
Systems
C25.1
WATER
Model
Base
Construction
Cost
Analysis
for
Sulfuric
Acid
Feed
Systems
C25.2
Base
Costs
Obtained
from
the
WATER
Model
for
Tube
Settling
Modules
C26.1
WATER
Model
Base
Construction
Cost
Analysis
for
Tube
Settling
Modules
C26.2
Base
Costs
Obtained
from
the
WATER
Model
for
Wash
Water
Surge
Basins
C27.1
WATER
Model
Base
Construction
Cost
Analysis
for
Wash
Water
Surge
Basins
C27.2
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
June
2003
C­
3
Below
is
an
explanation
of
the
abbreviations
used
in
this
appendix:

p
­
The
cost
belongs
to
the
process
cost
category
of
capital
cost
breakdown
c
­
The
cost
belongs
to
the
construction
cost
category
of
the
capital
cost
breakdown
e
­
The
cost
belongs
to
the
engineering
cost
category
of
the
capital
cost
breakdown
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C1.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Activated
Alumina
Plant
Capacity
(
mgd)
0.7
2.0
6.8
27
54
135
Manufactured
Equipment
$
26,760
$
44,580
$
138,330
$
522,210
$
1,031,270
$
2,564,560
p
Activated
Alumina
$
8,300
$
14,770
$
83,080
$
332,310
$
664,610
$
1,661,530
p
Labor
$
10,280
$
13,490
$
48,010
$
192,020
$
384,060
$
1,282,370
c
Pipes
and
Valves
$
16,260
$
19,320
$
69,030
$
273,210
$
542,650
$
1,368,060
p
Electrical
$
10,050
$
11,360
$
22,300
$
60,300
$
119,030
$
284,750
p
Housing
$
6,960
$
27,630
$
62,120
$
210,980
$
374,840
$
744,320
p
Contingencies
$
11,790
$
19,670
$
63,430
$
238,650
$
467,470
$
1,185,840
c
Total
$
90,400
$
150,820
$
486,300
$
1,829,680
$
3,583,930
$
9,091,430
Exhibit
C1.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Activated
Alumina
Plant
Capacity
(
mgd)
0.7
2.0
6.8
27
54
135
Manufactured
Equipment
29.60%
29.56%
28.45%
28.54%
28.77%
28.21%
28.86%
Activated
Alumina
9.18%
9.79%
17.08%
18.16%
18.54%
18.28%
15.17%
Labor
11.37%
8.94%
9.87%
10.49%
10.72%
14.11%
10.92%
Pipes
and
Valves
17.99%
12.81%
14.19%
14.93%
15.14%
15.05%
15.02%
Electrical
11.12%
7.53%
4.59%
3.30%
3.32%
3.13%
5.50%
Housing
7.70%
18.32%
12.77%
11.53%
10.46%
8.19%
11.49%
Contingencies
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
4
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C2.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Ammonia
Feed
Systems
Feed
Capacity
(
lb/
day)
250
500
1,000
2,500
5,000
Manufactured
Equipment
$
13,260
$
19,520
$
30,450
$
38,830
$
59,200
p
Labor
$
3,990
$
5,680
$
9,250
$
10,620
$
13,870
c
Pipes
and
Valves
$
2,390
$
3,520
$
5,500
$
7,000
$
10,670
p
Electrical
$
3,250
$
3,770
$
6,180
$
8,480
$
10,990
p
Housing
$
4,500
$
4,500
$
4,500
$
4,500
$
6,430
p
Contingencies
$
4,110
$
5,550
$
8,380
$
10,410
$
15,170
c
Total
$
31,500
$
42,540
$
64,260
$
79,840
$
116,330
Exhibit
C2.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Ammonia
Feed
Systems
Feed
Capacity
(
lb/
day)
250
500
1,000
2,500
5,000
Manufactured
Equipment
42.10%
45.89%
47.39%
48.63%
50.89%
46.98%
Labor
12.67%
13.35%
14.39%
13.30%
11.92%
13.13%
Pipes
and
Valves
7.59%
8.27%
8.56%
8.77%
9.17%
8.47%
Electrical
10.32%
8.86%
9.62%
10.62%
9.45%
9.77%
Housing
14.29%
10.58%
7.00%
5.64%
5.53%
8.61%
Contingencies
13.05%
13.05%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
5
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C3.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Backwash
Water
Pumping
Pumping
Capacity
(
mgd(
gpm))
1,260
(
1.8)
3,150
(
4.5)
6,300
(
9.1)
18,000
(
25.9)
22,950
(
33)
Manufactured
Equipment
$
11,400
$
14,600
$
38,380
$
76,780
$
95,970
p
Labor
$
3,050
$
4,410
$
4,880
$
9,290
$
12,440
c
Pipes
and
Valves
$
9,780
$
17,690
$
17,690
$
33,390
$
44,780
p
Electrical
$
13,350
$
16,040
$
16,740
$
28,070
$
33,250
p
Contingencies
$
5,640
$
7,910
$
11,650
$
22,130
$
27,970
c
Total
$
43,220
$
60,650
$
89,340
$
169,660
$
214,410
Exhibit
C3.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Backwash
Water
Pumping
Pumping
Capacity
(
mgd(
gpm))
1,260
(
1.8)
3,150
(
4.5)
6,300
(
9.1)
18,000
(
25.9)
22,950
(
33)
Manufactured
Equipment
26.38%
24.07%
42.96%
45.26%
44.76%
36.68%
Labor
7.06%
7.27%
5.46%
5.48%
5.80%
6.21%
Pipes
and
Valves
22.63%
29.17%
19.80%
19.68%
20.89%
22.43%
Electrical
30.89%
26.45%
18.74%
16.54%
15.51%
21.63%
Contingencies
13.05%
13.04%
13.04%
13.04%
13.05%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
6
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C4.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Chemical
Sludge
Pumping
Capacity
(
gpm)
20
100
500
1,000
5,000
10,000
Excavation
&
Sitework
$
470
$
600
$
810
$
970
$
1,840
$
2,220
c
Manufactured
Equipment
$
4,370
$
6,230
$
8,210
$
10,390
$
23,320
$
38,440
p
Concrete
$
1,500
$
2,210
$
3,220
$
4,100
$
9,270
$
12,310
p
Steel
$
1,510
$
2,130
$
3,120
$
3,940
$
8,640
$
11,070
p
Labor
$
5,280
$
8,060
$
12,880
$
17,400
$
47,850
$
64,720
c
Pipes
and
Valves
$
2,560
$
4,570
$
10,870
$
18,190
$
42,810
$
79,060
p
Electrical
$
6,290
$
7,390
$
7,880
$
9,380
$
10,380
$
12,510
p
Housing
$
5,880
$
5,880
$
5,880
$
8,100
$
8,100
$
11,700
p
Contingencies
$
4,180
$
5,560
$
7,930
$
10,870
$
22,830
$
34,800
c
Total
$
32,040
$
42,630
$
60,800
$
83,340
$
175,040
$
266,830
Exhibit
C4.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Chemical
Sludge
Pumping
Capacity
(
gpm)
20
100
500
1,000
5,000
10,000
Excavation
&
Sitework
1.47%
1.41%
1.33%
1.16%
1.05%
0.83%
1.21%
Manufactured
Equipment
13.64%
14.61%
13.50%
12.47%
13.32%
14.41%
13.66%
Concrete
4.68%
5.18%
5.30%
4.92%
5.30%
4.61%
5.00%
Steel
4.71%
5.00%
5.13%
4.73%
4.94%
4.15%
4.78%
Labor
16.48%
18.91%
21.18%
20.88%
27.34%
24.26%
21.51%
Pipes
and
Valves
7.99%
10.72%
17.88%
21.83%
24.46%
29.63%
18.75%
Electrical
19.63%
17.34%
12.96%
11.26%
5.93%
4.69%
11.97%
Housing
18.35%
13.79%
9.67%
9.72%
4.63%
4.38%
10.09%
Contingencies
13.05%
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
7
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C5.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Chlorination
Chlorine
Feed
Capacity
(
lb/
day)
10
500
1,000
2,000
5,000
10,000
Manufactured
Equipment
$
6,760
$
21,630
$
41,630
$
65,950
$
76,780
$
114,360
p
Labor
$
820
$
2,610
$
5,030
$
7,960
$
9,270
$
13,810
c
Pipes
and
Valves
$
540
$
1,710
$
3,300
$
5,230
$
6,080
$
9,060
p
Electrical
$
770
$
2,450
$
4,710
$
7,460
$
8,690
$
12,940
p
Housing
$
2,430
$
18,360
$
27,760
$
46,550
$
100,440
$
186,490
p
Contingencies
$
1,700
$
7,010
$
12,360
$
19,970
$
30,190
$
50,500
c
Total
$
13,020
$
53,770
$
94,790
$
153,120
$
231,450
$
387,160
Exhibit
C5.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Chlorination
Chlorine
Feed
Capacity
(
lb/
day)
10
500
1,000
2,000
5,000
10,000
Manufactured
Equipment
51.92%
40.23%
43.92%
43.07%
33.17%
29.54%
40.31%
Labor
6.30%
4.85%
5.31%
5.20%
4.01%
3.57%
4.87%
Pipes
and
Valves
4.15%
3.18%
3.48%
3.42%
2.63%
2.34%
3.20%
Electrical
5.91%
4.56%
4.97%
4.87%
3.75%
3.34%
4.57%
Housing
18.66%
34.15%
29.29%
30.40%
43.40%
48.17%
34.01%
Contingencies
13.06%
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
8
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C6.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Circular
Clarifiers
Surface
Area
(
SA=
ft2)
and
Diameter
(
D=
ft)
SA=
707
D=
30
SA=
1,590
D=
45
SA=
5,027
D=
80
SA=
10,387
D=
115
SA=
15,393
D=
140
SA=
22,698
D=
170
SA=
31,416
D=
200
Excavation
&
Sitework
$
1,530
$
2,430
$
4,900
$
7,860
$
10,280
$
13,520
$
17,130
c
Manufactured
Equipment
$
28,740
$
34,410
$
69,580
$
97,180
$
132,350
$
189,060
$
226,980
p
Concrete
$
4,860
$
7,710
$
15,480
$
24,800
$
32,400
$
42,560
$
53,860
p
Steel
$
14,160
$
21,090
$
67,240
$
129,250
$
188,720
$
249,570
$
335,140
p
Labor
$
10,770
$
16,180
$
30,960
$
46,980
$
60,110
$
77,640
$
96,320
c
Pipes
and
Valves
$
8,090
$
8,420
$
11,540
$
15,660
$
21,590
$
26,590
$
42,520
p
Electrical
$
5,940
$
5,940
$
7,560
$
8,270
$
10,870
$
12,370
$
13,060
p
Contingencies
$
11,110
$
14,430
$
31,090
$
49,500
$
68,450
$
91,700
$
117,750
c
Total
$
85,200
$
110,610
$
238,350
$
379,500
$
524,770
$
703,010
$
902,760
Exhibit
C6.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Circular
Clarifiers
Surface
Area
(
SA=
ft2)
and
Diameter
(
D=
ft)
SA=
707
D=
30
SA=
1,590
D=
45
SA=
5,027
D=
80
SA=
10,387
D=
115
SA=
15,393
D=
140
SA=
22,698
D=
170
SA=
31,416
D=
200
Excavation
&
Sitework
1.80%
2.20%
2.06%
2.07%
1.96%
1.92%
1.90%
1.99%
Manufactured
Equipment
33.73%
31.11%
29.19%
25.61%
25.22%
26.89%
25.14%
28.13%
Concrete
5.70%
6.97%
6.49%
6.53%
6.17%
6.05%
5.97%
6.27%
Steel
16.62%
19.07%
28.21%
34.06%
35.96%
35.50%
37.12%
29.51%
Labor
12.64%
14.63%
12.99%
12.38%
11.45%
11.04%
10.67%
12.26%
Pipes
and
Valves
9.50%
7.61%
4.84%
4.13%
4.11%
3.78%
4.71%
5.53%
Electrical
6.97%
5.37%
3.17%
2.18%
2.07%
1.76%
1.45%
3.28%
Contingencies
13.04%
13.05%
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
9
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C7.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Clearwell
Storage
Capacity
(
gal)
10,000
50,000
100,000
500,000
1,000,000
7,500,000
Excavation
&
Sitework
$
140
$
190
$
410
$
2,030
$
19,440
$
30,020
c
Concrete
$
8,250
$
14,430
$
23,280
$
66,330
$
105,520
$
622,500
p
Steel
$
5,700
$
9,240
$
14,550
$
32,670
$
113,050
$
350,700
p
Labor
$
13,050
$
21,480
$
35,040
$
84,090
$
109,290
$
394,160
p
Electrical
$
1,270
$
1,270
$
6,010
$
6,010
$
9,800
$
9,800
p
Contingencies
$
4,260
$
6,990
$
11,890
$
28,670
$
53,570
$
211,080
c
Total
$
32,670
$
53,600
$
91,180
$
219,800
$
410,670
$
1,618,260
Exhibit
C7.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Clearwell
Storage
Capacity
(
gal)
10,000
50,000
100,000
500,000
1,000,000
7,500,000
Excavation
&
Sitework
0.43%
0.35%
0.45%
0.92%
4.73%
1.86%
1.46%
Concrete
25.25%
26.92%
25.53%
30.18%
25.69%
38.47%
28.67%
Steel
17.45%
17.24%
15.96%
14.86%
27.53%
21.67%
19.12%
Labor
39.94%
40.07%
38.43%
38.26%
26.61%
24.36%
34.61%
Electrical
3.89%
2.37%
6.59%
2.73%
2.39%
0.61%
3.10%
Contingencies
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
10
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C8.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Ferric
Chloride
Feed
Systems*

Feed
Capacity
(
lb/
hr)
10.7
107
1,070
5,350
Manufactured
Equipment
$
7,500
$
13,100
$
33,560
$
160,940
p
Labor
$
420
$
1,130
$
2,430
$
12,160
c
Pipes
and
Valves
$
2,000
$
2,500
$
3,000
$
15,000
p
Electrical
$
1,110
$
2,260
$
4,960
$
19,000
p
Housing
$
6,000
$
13,300
$
51,270
$
174,590
p
Contingencies
$
2,550
$
4,840
$
14,280
$
57,250
c
Total
$
19,580
$
37,130
$
109,500
$
438,940
*
Numbers
were
unavailable
for
ferric
chloride.
However,
numbers
presented
for
ferrous
sulfate
and
ferric


sulfate
were
identical.

It
was
assumed
that
these
same
relationships
apply
to
ferric
chloride
Exhibit
C8.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Ferric
Chloride
Feed
Systems*

Feed
Capacity
(
lb/
hr)
10.7
107
1,070
5,350
Manufactured
Equipment
38.30%
35.28%
30.65%
36.67%
35.22%
Labor
2.15%
3.04%
2.22%
2.77%
2.54%
Pipes
and
Valves
10.21%
6.73%
2.74%
3.42%
5.78%
Electrical
5.67%
6.09%
4.53%
4.33%
5.15%
Housing
30.64%
35.82%
46.82%
39.78%
38.27%
Contingencies
13.02%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%

*
Numbers
were
unavailable
for
ferric
chloride.
However,
numbers
presented
for
ferrous
sulfate
and
ferric


sulfate
were
identical.

It
was
assumed
that
these
same
relationships
apply
to
ferric
chloride
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
11
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C9.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Finished
Water
Pumping
Plant
Capacity
(
mgd)
1.5
15
150
300
Manufactured
Equipment
$
15,410
$
89,700
$
567,600
$
1,142,350
p
Labor
$
3,880
$
11,580
$
80,400
$
158,840
c
Pipes
and
Valves
$
5,200
$
16,570
$
139,200
$
270,100
p
Electrical
$
7,180
$
38,450
$
210,490
$
400,230
p
Contingencies
$
4,750
$
23,450
$
149,650
$
295,730
c
Total
$
36,420
$
179,750
$
1,147,340
$
2,267,250
Exhibit
C9.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Finished
Water
Pumping
Plant
Capacity
(
mgd)
1.5
15
150
300
Manufactured
Equipment
42.31%
49.90%
49.47%
50.38%
48.02%
Labor
10.65%
6.44%
7.01%
7.01%
7.78%
Pipes
and
Valves
14.28%
9.22%
12.13%
11.91%
11.89%
Electrical
19.71%
21.39%
18.35%
17.65%
19.28%
Contingencies
13.04%
13.05%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
12
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C10.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Gravity
Filtration
Total
Filter
Area
(
FA­
ft2)
and
Plant
Flow
(
Q=
mgd)
FA=
140
Q=
1
FA=
700
Q=
5
FA=
1,400
Q=
10
FA=
7,000
Q=
50
FA=
14,000
Q=
100
FA=
28,000
Q=
200
Excavation
&
Sitework
$
1,950
$
3,620
$
5,520
$
16,220
$
25,590
$
43,410
c
Manufactured
Equipment
$
26,360
$
56,960
$
78,300
$
305,170
$
529,360
$
982,390
p
Concrete
$
13,400
$
27,040
$
41,660
$
95,490
$
154,790
$
275,570
p
Steel
$
11,550
$
19,960
$
30,120
$
73,530
$
123,160
$
209,960
p
Labor
$
40,580
$
88,490
$
150,870
$
356,380
$
508,980
$
1,000,670
c
Pipes
and
Valves
$
20,580
$
79,020
$
127,340
$
420,670
$
590,150
$
1,125,500
p
Electrical
$
13,390
$
38,410
$
38,410
$
99,140
$
168,840
$
265,310
p
Housing
$
17,400
$
40,480
$
70,590
$
291,940
$
514,330
$
968,520
p
Contingencies
$
21,780
$
53,100
$
81,420
$
248,780
$
392,280
$
730,700
c
Total
$
166,990
$
407,080
$
624,230
$
1,907,320
$
3,007,480
$
5,602,030
Exhibit
C10.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Gravity
Filtration
Total
Filter
Area
(
FA­
ft2)
and
Plant
Flow
(
Q=
mgd)
FA=
140
Q=
1
FA=
700
Q=
5
FA=
1,400
Q=
10
FA=
7,000
Q=
50
FA=
14,000
Q=
100
FA=
28,000
Q=
200
Excavation
&
Sitework
1.17%
0.89%
0.88%
0.85%
0.85%
0.77%
0.90%
Manufactured
Equipment
15.79%
13.99%
12.54%
16.00%
17.60%
17.54%
15.58%
Concrete
8.02%
6.64%
6.67%
5.01%
5.15%
4.92%
6.07%
Steel
6.92%
4.90%
4.83%
3.86%
4.10%
3.75%
4.72%
Labor
24.30%
21.74%
24.17%
18.68%
16.92%
17.86%
20.61%
Pipes
and
Valves
12.32%
19.41%
20.40%
22.06%
19.62%
20.09%
18.98%
Electrical
8.02%
9.44%
6.15%
5.20%
5.61%
4.74%
6.53%
Housing
10.42%
9.94%
11.31%
15.31%
17.10%
17.29%
13.56%
Contingencies
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
13
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C11.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Horizontal
Paddle,
G=
50
Total
Basin
Volume
(
ft3)
1,800
10,000
25,000
100,000
500,000
1,000,000
Excavation
&
Sitework
$
470
$
2,550
$
4,290
$
9,970
$
40,080
$
77,640
p
Manufactured
Equipment
$
12,140
$
28,250
$
35,410
$
74,400
$
220,800
$
433,640
p
Concrete
$
1,400
$
7,610
$
12,740
$
29,770
$
120,280
$
232,960
p
Steel
$
2,360
$
12,550
$
20,440
$
46,500
$
175,290
$
339,510
p
Labor
$
7,080
$
20,220
$
29,420
$
75,460
$
221,200
$
439,770
c
Electrical
$
6,980
$
28,320
$
28,320
$
28,320
$
141,610
$
283,220
p
Contingencies
$
4,560
$
14,930
$
19,590
$
39,660
$
137,890
$
271,010
c
Total
$
34,990
$
114,430
$
150,210
$
304,080
$
1,057,150
$
2,077,750
Exhibit
C11.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Horizontal
Paddle,
G=
50
Total
Basin
Volume
(
ft3)
1,800
10,000
25,000
100,000
500,000
1,000,000
Excavation
&
Sitework
1.34%
2.23%
2.86%
3.28%
3.79%
3.74%
2.87%
Manufactured
Equipment
34.70%
24.69%
23.57%
24.47%
20.89%
20.87%
24.86%
Concrete
4.00%
6.65%
8.48%
9.79%
11.38%
11.21%
8.59%
Steel
6.74%
10.97%
13.61%
15.29%
16.58%
16.34%
13.26%
Labor
20.23%
17.67%
19.59%
24.82%
20.92%
21.17%
20.73%
Electrical
19.95%
24.75%
18.85%
9.31%
13.40%
13.63%
16.65%
Contingencies
13.03%
13.05%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
14
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C12.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Horizontal
Paddle,
G=
80
Total
Basin
Volume
(
ft3)
1,800
10,000
25,000
100,000
500,000
Excavation
&
Sitework
$
470
$
2,550
$
4,290
$
9,970
$
40,080
c
Manufactured
Equipment
$
12,140
$
34,210
$
44,360
$
115,770
$
427,670
p
Concrete
$
1,400
$
7,610
$
12,740
$
29,770
$
120,280
p
Steel
$
2,360
$
12,550
$
20,440
$
46,500
$
175,290
p
Labor
$
7,080
$
22,190
$
32,370
$
90,170
$
289,520
p
Electrical
$
6,980
$
28,320
$
28,320
$
28,320
$
141,610
p
Contingencies
$
4,560
$
16,110
$
21,380
$
48,080
$
179,170
c
Total
$
34,990
$
123,540
$
163,900
$
368,580
$
1,373,620
Exhibit
C12.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Horizontal
Paddle,
G=
80
Total
Basin
Volume
(
ft3)
1,800
10,000
25,000
100,000
500,000
Excavation
&
Sitework
1.34%
2.06%
2.62%
2.70%
2.92%
2.33%
Manufactured
Equipment
34.70%
27.69%
27.07%
31.41%
31.13%
30.40%
Concrete
4.00%
6.16%
7.77%
8.08%
8.76%
6.95%
Steel
6.74%
10.16%
12.47%
12.62%
12.76%
10.95%
Labor
20.23%
17.96%
19.75%
24.46%
21.08%
20.70%
Electrical
19.95%
22.92%
17.28%
7.68%
10.31%
15.63%
Contingencies
13.03%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
15
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C13.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Hydraulic
Surface
Wash
Total
Filter
Area
(
ft2)
140
700
1,400
7,000
14,000
28,000
Manufactured
Equipment
$
9,170
$
12,050
$
35,090
$
82,010
$
172,440
$
401,200
p
Labor
$
1,300
$
2,770
$
5,170
$
14,710
$
29,430
$
66,600
c
Pipes
and
Valves
$
2,570
$
5,100
$
7,020
$
13,390
$
32,290
$
59,870
p
Electrical
$
12,670
$
17,920
$
20,440
$
37,900
$
61,120
$
92,360
p
Contingencies
$
3,860
$
5,680
$
10,160
$
22,200
$
44,290
$
93,000
c
Total
$
29,570
$
43,520
$
77,880
$
170,210
$
339,570
$
713,030
Exhibit
C13.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Hydraulic
Surface
Wash
Total
Filter
Area
(
ft2)
140
700
1,400
7,000
14,000
28,000
Manufactured
Equipment
31.01%
27.69%
45.06%
48.18%
50.78%
56.27%
43.16%
Labor
4.40%
6.36%
6.64%
8.64%
8.67%
9.34%
7.34%
Pipes
and
Valves
8.69%
11.72%
9.01%
7.87%
9.51%
8.40%
9.20%
Electrical
42.85%
41.18%
26.25%
22.27%
18.00%
12.95%
27.25%
Contingencies
13.05%
13.05%
13.05%
13.04%
13.04%
13.04%
13.05%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
16
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C14.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
In­
Plant
Pumping
Pumping
Capacity
(
mgd)
1
5
10
50
100
200
Excavation
&
Sitework
$
100
$
100
$
130
$
360
$
600
$
1,030
c
Manufactured
Equipment
$
6,300
$
9,110
$
14,780
$
48,650
$
83,400
$
152,900
p
Concrete
$
970
$
970
$
1,510
$
4,770
$
8,030
$
14,090
p
Steel
$
1,610
$
1,610
$
2,450
$
7,630
$
12,500
$
21,330
p
Labor
$
5,570
$
10,410
$
24,070
$
63,330
$
129,130
$
331,030
c
Pipes
and
Valves
$
5,090
$
12,330
$
16,300
$
60,230
$
114,200
$
222,080
p
Electrical
$
3,170
$
4,930
$
7,390
$
25,760
$
47,240
$
89,360
p
Housing
$
1,500
$
1,500
$
3,000
$
14,520
$
28,830
$
58,080
p
Contingencies
$
3,650
$
6,140
$
10,440
$
33,790
$
63,590
$
133,490
c
Total
$
27,960
$
47,100
$
80,070
$
259,040
$
487,520
$
1,023,390
Exhibit
C14.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
In­
Plant
Pumping
Pumping
Capacity
(
mgd)
1
5
10
50
100
200
Excavation
&
Sitework
0.36%
0.21%
0.16%
0.14%
0.12%
0.10%
0.18%
Manufactured
Equipment
22.53%
19.34%
18.46%
18.78%
17.11%
14.94%
18.53%
Concrete
3.47%
2.06%
1.89%
1.84%
1.65%
1.38%
2.05%
Steel
5.76%
3.42%
3.06%
2.95%
2.56%
2.08%
3.31%
Labor
19.92%
22.10%
30.06%
24.45%
26.49%
32.35%
25.89%
Pipes
and
Valves
18.20%
26.18%
20.36%
23.25%
23.42%
21.70%
22.19%
Electrical
11.34%
10.47%
9.23%
9.94%
9.69%
8.73%
9.90%
Housing
5.36%
3.18%
3.75%
5.61%
5.91%
5.68%
4.92%
Contingencies
13.05%
13.04%
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
17
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C15.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Ion
Exchange
Plant
Capacity
(
mgd)
1.1
3.7
6.1
12.3
Excavation
&
Sitework
$
740
$
1,140
$
1,470
$
1,970
c
Manufactured
Equipment
$
39,960
$
89,580
$
137,770
$
258,230
p
Media
$
92,790
$
313,160
$
521,940
$
1,043,880
p
Concrete
$
2,410
$
3,580
$
4,750
$
6,320
p
Steel
$
3,830
$
5,680
$
7,530
$
9,950
p
Labor
$
17,420
$
33,510
$
61,460
$
125,080
c
Pipes
and
Valves
$
14,040
$
38,780
$
69,740
$
139,480
p
Electrical
$
27,700
$
38,510
$
60,820
$
120,210
p
Housing
$
21,920
$
35,660
$
57,440
$
79,820
p
Contingencies
$
33,120
$
83,940
$
138,440
$
267,740
c
Total
$
253,930
$
643,540
$
1,061,360
$
2,052,680
Exhibit
C15.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Ion
Exchange
Plant
Capacity
(
mgd)
1.1
3.7
6.1
12.3
Excavation
&
Sitework
0.29%
0.18%
0.14%
0.10%
0.18%
Manufactured
Equipment
15.74%
13.92%
12.98%
12.58%
13.80%
Media
36.54%
48.66%
49.18%
50.85%
46.31%
Concrete
0.95%
0.56%
0.45%
0.31%
0.57%
Steel
1.51%
0.88%
0.71%
0.48%
0.90%
Labor
6.86%
5.21%
5.79%
6.09%
5.99%
Pipes
and
Valves
5.53%
6.03%
6.57%
6.80%
6.23%
Electrical
10.91%
5.98%
5.73%
5.86%
7.12%
Housing
8.63%
5.54%
5.41%
3.89%
5.87%
Contingencies
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
18
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C16.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Lime
Feed
with
Recalcination
Feed
Capacity
(
lb/
hr)
1,000
10,000
Manufactured
Equipment
$
48,870
$
80,660
p
Labor
$
1,510
$
3,060
c
Pipes
and
Valves
$
3,120
$
6,250
p
Electrical
$
6,880
$
12,320
p
Housing
$
9,450
$
26,250
p
Contingencies
$
10,470
$
19,280
c
Total
$
80,300
$
147,820
Exhibit
C16.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Lime
Feed
with
Recalcination
Feed
Capacity
(
lb/
hr)
1,000
10,000
Manufactured
Equipment
60.86%
54.57%
57.71%
Labor
1.88%
2.07%
1.98%
Pipes
and
Valves
3.89%
4.23%
4.06%
Electrical
8.57%
8.33%
8.45%
Housing
11.77%
17.76%
14.76%
Contingencies
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
19
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C17.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Permanganate
Feed
Systems
Feed
Capacity
(
lb/
day)
1
10
100
500
Manufactured
Equipment
$
2,340
$
2,600
$
3,380
$
5,220
p
Labor
$
480
$
480
$
540
$
770
c
Pipes
and
Valves
$
970
$
970
$
970
$
970
p
Electrical
$
3,190
$
3,190
$
3,190
$
3,190
p
Housing
$
1,260
$
1,580
$
1,950
$
2,940
p
Contingencies
$
1,240
$
1,320
$
1,500
$
1,960
c
Total
$
9,480
$
10,140
$
11,530
$
15,050
Exhibit
C17.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Permanganate
Feed
Systems
Feed
Capacity
(
lb/
day)
1
10
100
500
Manufactured
Equipment
24.68%
25.64%
29.31%
34.68%
28.58%
Labor
5.06%
4.73%
4.68%
5.12%
4.90%
Pipes
and
Valves
10.23%
9.57%
8.41%
6.45%
8.66%
Electrical
33.65%
31.46%
27.67%
21.20%
28.49%
Housing
13.29%
15.58%
16.91%
19.53%
16.33%
Contingencies
13.08%
13.02%
13.01%
13.02%
13.03%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
20
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C18.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Polymer
Feed
Systems
Feed
Capacity
(
lb/
hr)
1
10
100
200
Manufactured
Equipment
$
11,670
$
11,670
$
14,730
$
18,970
p
Labor
$
700
$
700
$
700
$
760
c
Pipes
and
Valves
$
280
$
280
$
280
$
300
p
Electrical
$
1,290
$
1,290
$
1,290
$
1,290
p
Housing
$
3,600
$
3,600
$
4,050
$
4,500
p
Contingencies
$
2,630
$
2,630
$
3,160
$
3,870
c
Total
$
20,170
$
20,170
$
24,210
$
29,690
Exhibit
C18.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Polymer
Feed
Systems
Feed
Capacity
(
lb/
hr)
1
10
100
200
Manufactured
Equipment
57.86%
57.86%
60.84%
63.89%
60.11%
Labor
3.47%
3.47%
2.89%
2.56%
3.10%
Pipes
and
Valves
1.39%
1.39%
1.16%
1.01%
1.24%
Electrical
6.40%
6.40%
5.33%
4.34%
5.62%
Housing
17.85%
17.85%
16.73%
15.16%
16.90%
Contingencies
13.04%
13.04%
13.05%
13.03%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
21
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C19.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Rapid
Mix,
G=
900
Basin
Volume
(
ft3)
100
500
1,000
5,000
10,000
20,000
Excavation
&
Sitework
$
220
$
380
$
490
$
1,360
$
2,720
$
5,460
c
Manufactured
Equipment
$
4,310
$
9,830
$
14,760
$
66,840
$
133,670
$
267,340
p
Concrete
$
390
$
870
$
1,280
$
3,610
$
7,220
$
14,450
p
Steel
$
570
$
1,350
$
2,010
$
5,600
$
11,180
$
22,360
p
Labor
$
1,230
$
2,300
$
3,410
$
13,140
$
26,280
$
52,550
c
Electrical
$
6,980
$
6,980
$
7,180
$
7,470
$
8,760
$
16,100
p
Contingencies
$
2,060
$
3,260
$
4,370
$
14,700
$
28,470
$
56,740
c
Total
$
15,760
$
24,970
$
33,500
$
112,720
$
218,300
$
435,000
Exhibit
C19.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Rapid
Mix,
G=
900
Basin
Volume
(
ft3)
100
500
1,000
5,000
10,000
20,000
Excavation
&
Sitework
1.40%
1.52%
1.46%
1.21%
1.25%
1.26%
1.35%
Manufactured
Equipment
27.35%
39.37%
44.06%
59.30%
61.23%
61.46%
48.79%
Concrete
2.47%
3.48%
3.82%
3.20%
3.31%
3.32%
3.27%
Steel
3.62%
5.41%
6.00%
4.97%
5.12%
5.14%
5.04%
Labor
7.80%
9.21%
10.18%
11.66%
12.04%
12.08%
10.50%
Electrical
44.29%
27.95%
21.43%
6.63%
4.01%
3.70%
18.00%
Contingencies
13.07%
13.06%
13.04%
13.04%
13.04%
13.04%
13.05%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
22
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C20.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Recarbonation,
Liquid
Carbon
Dioxide
Installed
Capacity
(
lb/
day)
380
750
1,500
3,750
7,500
15,000
Manufactured
Equipment
$
27,000
$
31,000
$
35,250
$
49,250
$
73,000
$
141,000
p
Labor
$
7,650
$
8,780
$
12,170
$
17,330
$
28,990
$
58,010
c
Pipes
and
Valves
$
1,530
$
2,340
$
4,620
$
8,710
$
16,940
$
37,540
p
Housing
$
7,360
$
7,360
$
7,360
$
7,360
$
8,450
$
8,900
p
Contingencies
$
6,530
$
7,420
$
8,910
$
12,400
$
19,110
$
36,820
c
Total
$
50,070
$
56,900
$
68,310
$
95,050
$
146,490
$
282,270
Exhibit
C20.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Recarbonation,
Liquid
Carbon
Dioxide
Installed
Capacity
(
lb/
day)
380
750
1,500
3,750
7,500
15,000
Manufactured
Equipment
53.92%
54.48%
51.60%
51.81%
49.83%
49.95%
51.93%
Labor
15.28%
15.43%
17.82%
18.23%
19.79%
20.55%
17.85%
Pipes
and
Valves
3.06%
4.11%
6.76%
9.16%
11.56%
13.30%
7.99%
Housing
14.70%
12.93%
10.77%
7.74%
5.77%
3.15%
9.18%
Contingencies
13.04%
13.04%
13.04%
13.05%
13.05%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
23
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C21.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Recarbonation
Basins
Single
Basin
Volume
(
ft3)
770
1,375
2,750
5,630
8,800
17,600
35,200
Excavation
&
Sitework
$
520
$
620
$
980
$
1,390
$
1,790
$
3,050
$
5,570
c
Concrete
$
1,380
$
1,860
$
2,820
$
4,050
$
5,190
$
8,570
$
15,320
p
Steel
$
2,250
$
3,010
$
4,670
$
6,560
$
8,320
$
13,960
$
25,240
p
Labor
$
2,830
$
3,800
$
5,730
$
8,090
$
10,240
$
16,740
$
29,730
c
Pipes
and
Valves
$
90
$
130
$
250
$
480
$
680
$
1,360
$
3,360
p
Contingencies
$
1,060
$
1,410
$
2,170
$
3,090
$
3,930
$
6,550
$
11,880
c
Total
$
8,130
$
10,830
$
16,620
$
23,660
$
30,150
$
50,230
$
91,100
Exhibit
C21.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Recarbonation
Basins
Single
Basin
Volume
(
ft3)
770
1,375
2,750
5,630
8,800
17,600
35,200
Excavation
&
Sitework
6.40%
5.72%
5.90%
5.87%
5.94%
6.07%
6.11%
6.00%
Concrete
16.97%
17.17%
16.97%
17.12%
17.21%
17.06%
16.82%
17.05%
Steel
27.68%
27.79%
28.10%
27.73%
27.60%
27.79%
27.71%
27.77%
Labor
34.81%
35.09%
34.48%
34.19%
33.96%
33.33%
32.63%
34.07%
Pipes
and
Valves
1.11%
1.20%
1.50%
2.03%
2.26%
2.71%
3.69%
2.07%
Contingencies
13.04%
13.02%
13.06%
13.06%
13.03%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
24
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C22.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Rectangular
Clarifiers
Area
(
A=
ft2)
and
Length
x
Width
(
LW=
ftxft)
A=
240
LW=
30x8
A=
600
LW=
60x10
A=
1260
LW=
90x14
A=
2240
LW=
140x16
A=
3600
LW=
200x18
A=
4800
LW=
240x20
Excavation
&
Sitework
$
1,060
$
2,000
$
3,060
$
4,680
$
6,670
$
8,090
c
Manufactured
Equipment
$
8,540
$
12,080
$
24,470
$
32,020
$
53,110
$
63,440
p
Concrete
$
2,970
$
5,490
$
8,430
$
12,820
$
18,190
$
22,070
p
Steel
$
6,400
$
13,110
$
19,440
$
32,620
$
51,250
$
69,680
p
Labor
$
6,220
$
11,260
$
17,320
$
26,390
$
37,570
$
45,300
c
Pipes
and
Valves
$
6,960
$
7,400
$
9,100
$
12,500
$
16,100
$
21,450
p
Electrical
$
1,510
$
1,760
$
1,860
$
2,020
$
2,110
$
2,400
p
Contingencies
$
5,050
$
7,970
$
12,550
$
18,460
$
27,750
$
34,860
c
Total
$
38,710
$
61,070
$
96,230
$
141,510
$
212,750
$
267,290
Exhibit
C22.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Rectangular
Clarifiers
Area
(
A=
ft2)
and
Length
x
Width
(
LW=
ftxft)
A=
240
LW=
30x8
A=
600
LW=
60x10
A=
1260
LW=
90x14
A=
2240
LW=
140x16
A=
3600
LW=
200x18
A=
4800
LW=
240x20
Excavation
&
Sitework
2.74%
3.27%
3.18%
3.31%
3.14%
3.03%
3.11%
Manufactured
Equipment
22.06%
19.78%
25.43%
22.63%
24.96%
23.73%
23.10%
Concrete
7.67%
8.99%
8.76%
9.06%
8.55%
8.26%
8.55%
Steel
16.53%
21.47%
20.20%
23.05%
24.09%
26.07%
21.90%
Labor
16.07%
18.44%
18.00%
18.65%
17.66%
16.95%
17.63%
Pipes
and
Valves
17.98%
12.12%
9.46%
8.83%
7.57%
8.02%
10.66%
Electrical
3.90%
2.88%
1.93%
1.43%
0.99%
0.90%
2.01%
Contingencies
13.05%
13.05%
13.04%
13.05%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
25
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C23.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Reverse
Osmosis
Plant
Capacity
(
mgd)
1.0
10
100
200
Manufactured
Equipment
$
474,210
$
3,458,480
$
29,174,260
$
56,438,930
p
Labor
$
70,420
$
346,850
$
2,312,340
$
2,837,870
c
Electrical
$
65,740
$
486,270
$
3,635,690
$
6,947,480
p
Housing
$
64,260
$
462,650
$
2,409,660
$
4,176,740
p
Contingencies
$
101,190
$
713,140
$
5,629,790
$
10,560,150
c
Total
$
775,820
$
5,467,390
$
43,161,740
$
80,961,170
Exhibit
C23.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Reverse
Osmosis
Plant
Capacity
(
mgd)
1.0
10
100
200
Manufactured
Equipment
61.12%
63.26%
67.59%
69.71%
65.42%
Labor
9.08%
6.34%
5.36%
3.51%
6.07%
Electrical
8.47%
8.89%
8.42%
8.58%
8.59%
Housing
8.28%
8.46%
5.58%
5.16%
6.87%
Contingencies
13.04%
13.04%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
26
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C24.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Sodium
Hydroxide
Feed
Systems
Feed
Capacity
(
lb/
day)
10
100
1,000
10000
Manufactured
Equipment
$
6,440
$
7,010
$
5,720
$
19,450
p
Labor
$
640
$
640
$
790
$
4,120
c
Pipes
and
Valves
$
850
$
850
$
850
$
850
p
Electrical
$
3,190
$
3,190
$
3,190
$
3,460
p
Housing
$
1,010
$
2,100
$
8,400
$
48,380
p
Contingencies
$
1,820
$
2,070
$
2,840
$
11,440
c
Total
$
13,950
$
15,860
$
21,790
$
87,700
Exhibit
C24.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Sodium
Hydroxide
Feed
Systems
Feed
Capacity
(
lb/
day)
10
100
1,000
10,000
Manufactured
Equipment
46.16%
44.20%
26.25%
22.18%
34.70%
Labor
4.59%
4.04%
3.63%
4.70%
4.24%
Pipes
and
Valves
6.09%
5.36%
3.90%
0.97%
4.08%
Electrical
22.87%
20.11%
14.64%
3.95%
15.39%
Housing
7.24%
13.24%
38.55%
55.17%
28.55%
Contingencies
13.05%
13.05%
13.03%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
27
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C25.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Sulfuric
Acid
Feed
Systems
Feed
Capacity
(
gpd)
10
100
1000
5000
Manufactured
Equipment
$
1,560
$
3,440
$
12,400
$
41,000
p
Labor
$
640
$
820
$
2,840
$
11,840
c
Pipes
and
Valves
$
1,090
$
1,090
$
2,150
$
2,150
p
Electrical
$
1,670
$
2,920
$
2,920
$
2,920
p
Housing
$
2,520
$
1,560
$
1,560
$
1,560
p
Contingencies
$
1,120
$
1,470
$
3,280
$
8,920
c
Total
$
8,600
$
11,300
$
25,150
$
68,390
Exhibit
C25.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Sulfuric
Acid
Feed
Systems
Feed
Capacity
(
gpd)
10
100
1000
5000
Manufactured
Equipment
18.14%
30.44%
49.30%
59.95%
39.46%
Labor
7.44%
7.26%
11.29%
17.31%
10.83%
Pipes
and
Valves
12.67%
9.65%
8.55%
3.14%
8.50%
Electrical
19.42%
25.84%
11.61%
4.27%
15.28%
Housing
29.30%
13.81%
6.20%
2.28%
12.90%
Contingencies
13.02%
13.01%
13.04%
13.04%
13.03%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
28
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C26.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Tube
Settling
Modules
Tube
Module
Area
(
ft2)
280
2,800
14,000
28,000
56,000
Manufactured
Equipment
$
4,200
$
31,000
$
147,000
$
282,000
$
504,000
p
Steel
$
2,000
$
19,500
$
95,000
$
155,000
$
300,000
p
Labor
$
2,500
$
11,200
$
49,000
$
95,000
$
224,000
c
Contingencies
$
1,300
$
9,300
$
43,700
$
79,800
$
154,200
c
Total
$
10,000
$
71,000
$
334,700
$
611,800
$
1,182,200
Exhibit
C26.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Tube
Settling
Modules
Tube
Module
Area
(
ft2)
280
2,800
14,000
28,000
56,000
Manufactured
Equipment
42.00%
43.66%
43.92%
46.09%
42.63%
43.66%
Steel
20.00%
27.46%
28.38%
25.34%
25.38%
25.31%
Labor
25.00%
15.77%
14.64%
15.53%
18.95%
17.98%
Contingencies
13.00%
13.10%
13.06%
13.04%
13.04%
13.05%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
29
June
2003
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
By­
Products
Exhibit
C27.1
­
Base
Costs
Obtained
from
the
WATER
Model
for
Wash
Water
Surge
Basins
Capacity
(
gal)
10,000
50,000
100,000
500,000
Excavation
&
Sitework
$
200
$
520
$
1,250
$
4,400
c
Concrete
$
11,560
$
39,310
$
71,480
$
143,680
p
Steel
$
7,990
$
25,170
$
44,680
$
70,770
p
Labor
$
18,270
$
58,500
$
107,590
$
182,150
c
Pipes
and
Valves
$
5,500
$
7,500
$
11,000
$
16,000
p
Electrical
$
1,300
$
1,300
$
6,000
$
6,000
p
Contingencies
$
6,720
$
19,850
$
36,300
$
63,450
c
Total
$
51,540
$
152,150
$
278,300
$
486,450
Exhibit
C27.2
­
WATER
Model
Base
Construction
Cost
Analysis
for
Wash
Water
Surge
Basins
Capacity
(
gal)
10,000
50,000
100,000
500,000
Excavation
&
Sitework
0.39%
0.34%
0.45%
0.90%
0.52%
Concrete
22.43%
25.84%
25.68%
29.54%
25.87%
Steel
15.50%
16.54%
16.05%
14.55%
15.66%
Labor
35.45%
38.45%
38.66%
37.44%
37.50%
Pipes
and
Valves
10.67%
4.93%
3.95%
3.29%
5.71%
Electrical
2.52%
0.85%
2.16%
1.23%
1.69%
Contingencies
13.04%
13.05%
13.04%
13.04%
13.04%
Total
100.00%
100.00%
100.00%
100.00%
100.00%
Cost
Component
Capital
Cost
Category
Cost
Component
Average
Percent
C­
30
June
2003
Appendix
D
Technology
Cost
Curves
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
D­
1
June
2003
Appendix
D
Unit
Costs
Graphs
Costs
for
independent
flows
are
presented
in
the
main
text
of
this
document.
This
appendix
provides
graphs
of
those
points
and
displays
the
lines
that
were
used
to
predict
costs
for
flows
other
than
those
costed.
This
appendix
provides
the
following
information:

°
Capital
unit
cost
estimates
for
a
wide
range
of
design
flows
(
in
tabular
and
graphical
forms)
°
O&
M
unit
cost
estimates
for
a
wide
range
of
average
daily
flows
(
in
tabular
and
graphical
forms)

The
range
of
design
and
average
flows
is
intended
to
cover
all
possible
system
flows.
When
flows
fall
in
between
the
design
or
average
daily
flows
used
to
estimate
unit
costs,
straight
line
interpolation
can
be
used
to
estimate
the
capital
or
O&
M
cost.
Design
costs
were
calculated
for
points
ranging
between
0.007
MGD
and
520
MGD.
For
plants
with
flows
less
than
0.007
MGD
the
value
for
0.007
MGD
was
used.
For
plants
with
flows
greater
than
520
MGD,
the
costs
are
calculated
by
extrapolating
a
straight
line
between
the
last
two
calculated
cost
points.
Points
are
included
in
the
graphs
at
0.0001
MGD
and
1500
MGD
to
show
these
assumptions.
Likewise
for
average
daily
flows,
points
were
calculated
between
0.0015
MGD
and
350
MGD.
Points
outside
this
range
show
the
assumptions
used
to
extrapolate
costs.

The
Appendix
D
Contents
(
shown
on
the
next
page)
describes
the
exhibits
in
this
appendix.
Each
exhibit
lists
the
constraints
and
design
criteria
for
the
technology,
presents
a
table
showing
the
unit
cost
estimates
for
each
design
or
average
flow
point,
and
graphically
displays
each
point
to
illustrate
the
way
in
which
the
costs
increase
with
flow.
All
graphs
are
in
Log­
Log
scale.
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
D­
2
June
2003
Appendix
D
Contents
Technology
Cost
Type
Exhibit
Number
Chloramines
(
Ammonia
dose
=
0.55
mg/
L)
Capital
D.
1
O&
M
D.
2
Chloramines
(
Ammonia
dose
=
0.15
mg/
L)
Capital
D.
3
O&
M
D.
4
Chlorine
Dioxide
(
ClO
2
Dose
=
1.25
mg/
L)
Capital
D.
5
O&
M
D.
6
UV
(
40
mJ/
cm2)
Capital
D.
7
O&
M
D.
8
UV
(
200
mJ/
cm2)
Capital
D.
9
O&
M
D.
10
Ozone,
0.5­
Log
Inactivation
of
Cryptosporidium
Capital
D.
11
O&
M
D.
12
Ozone,
1.0­
Log
Inactivation
of
Cryptosporidium
Capital
D.
13
O&
M
D.
14
Ozone,
2.0­
Log
Inactivation
of
Cryptosporidium
Capital
D.
15
O&
M
D.
16
Microfiltration/
Ultrafiltration
(
MF/
UF)
Capital
D.
17
O&
M
D.
18
Bag
Filters
Capital
D.
19
O&
M
D.
20
Cartridge
Filters
Capital
D.
21
O&
M
D.
22
Bank
Filtration
Capital
D.
23
Second
Stage
Filtration
Capital
D.
24
O&
M
D.
25
Pre­
Sedimentation
with
Coagulant
Capital
D.
26
O&
M
D.
27
Watershed
Control
Capital
D.
28
O&
M
D.
29
Combined
Filter
Performance
Capital
D.
30
O&
M
D.
31
GAC10­
360
Capital
D.
32
O&
M
D.
33
GAC20­
90
Capital
D.
34
O&
M
D.
35
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
Technology
Cost
Type
Exhibit
Number
D­
3
June
2003
GAC20­
240
Capital
D.
36
O&
M
D.
37
Nanofiltration
Capital
D.
38
O&
M
D.
39
Constraints:
It
can
be
used
alone
or
in
conjunction
with
the
other
technologies
Design
Criteria:
1)
Ammonia
dose
=
0.55
mg/
L
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
27,912
0.0070
$
27,912
0.0220
$
27,912
0.0370
$
27,912
0.0910
$
27,912
0.1800
$
29,412
0.2700
$
36,440
0.3600
$
37,321
0.6800
$
40,454
1.0000
$
51,586
1.2000
$
80,696
2.0000
$
80,696
3.5000
$
80,696
7.0000
$
80,696
17.0000
$
95,696
22.0000
$
129,366
76.0000
$
382,253
210.0000
$
474,677
430.0000
$
570,244
520.0000
$
710,620
1,500.0000
$
2,239,158
Exhibit
D.
1
­
Capital
Costs
for
Switching
to
Chloramines
Surface
Water
Plants
Capital
Costs
for
Switching
to
Chloramines
(
Ammonia
dose
0.55
mg/
L)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.0001
0.0010
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
10,000.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
4
June
2003
Constraints:
It
can
be
used
alone
or
in
conjunction
with
the
other
technologies
Design
Criteria:
1)
Ammonia
dose
=
0.55
mg/
L
Average
Flow
O&
M
cost
(
mgd)
($)
0.0001
$
1,566
0.0015
$
1,566
0.0054
$
1,570
0.0095
$
1,575
0.0250
$
1,592
0.0540
$
1,623
0.0840
$
3,038
0.1100
$
3,065
0.2300
$
3,101
0.3500
$
4,478
0.4100
$
6,037
0.7700
$
6,678
1.4000
$
7,875
3.0000
$
10,263
7.8000
$
15,174
11.0000
$
18,601
38.0000
$
30,967
120.0000
$
79,369
270.0000
$
153,192
350.0000
$
195,454
750.0000
$
406,765
Exhibit
D.
2
­
O&
M
Costs
for
Switching
to
Chloramines
Surface
Water
Plants
O&
M
Costs
for
Switching
to
Chloramines
(
Ammonia
dose
0.55
mg/
L)

$
1,000
$
10,000
$
100,000
$
1,000,000
0.0000
0.0001
0.0010
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
5
June
2003
Constraints:
It
can
be
used
alone
or
in
conjunction
with
the
other
technologies
Design
Criteria:
1)
Ammonia
dose
=
0.15
mg/
L
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
27,912
0.0070
$
27,912
0.0220
$
27,912
0.0370
$
27,912
0.0910
$
27,912
0.1800
$
29,412
0.2700
$
36,440
0.3600
$
37,321
0.6800
$
40,454
1.0000
$
51,586
1.2000
$
80,696
2.0000
$
80,696
3.5000
$
80,696
7.0000
$
80,696
17.0000
$
95,696
22.0000
$
95,696
76.0000
$
95,696
210.0000
$
154,366
430.0000
$
413,127
520.0000
$
413,127
1,500.0000
$
413,127
Ground
Water
Plants
Exhibit
D.
3
­
Capital
Costs
for
Switching
to
Chloramines
Capital
Costs
for
Switching
to
Chloramines
(
Ammonia
Dose
0.15
mg/
L)

$
10,000
$
100,000
$
1,000,000
­
200.0000
400.0000
600.0000
800.0000
1,000.0000
1,200.0000
1,400.0000
1,600.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
6
June
2003
Constraints:
It
can
be
used
alone
or
in
conjunction
with
the
other
technologies
Design
Criteria:
1)
Ammonia
dose
=
0.15
mg/
L
Average
Flow
O&
M
Cost
(
mgd)
($)
0.0001
$
1,565
0.0015
$
1,565
0.0054
$
1,566
0.0095
$
1,567
0.0250
$
1,572
0.0540
$
1,580
0.0840
$
2,973
0.1100
$
2,981
0.2300
$
2,990
0.3500
$
4,310
0.4100
$
5,780
0.7700
$
6,196
1.4000
$
7,004
3.0000
$
8,415
7.8000
$
11,015
11.0000
$
12,534
38.0000
$
23,008
120.0000
$
45,384
270.0000
$
65,310
350.0000
$
77,901
750.0000
$
140,855
Exhibit
D.
4
­
O&
M
Costs
for
Switching
to
Chloramines
Ground
Water
Plants
O&
M
Costs
for
Switching
to
Chloramines
(
Ammonia
Dose
0.15
mg/
L)

$
1,000
$
10,000
$
100,000
$
1,000,000
­
100.0000
200.0000
300.0000
400.0000
500.0000
600.0000
700.0000
800.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
7
June
2003
Constraints:
Not
practical
for
systems
serving
500
or
fewer
people
Design
Criteria:
1)
ClO2
dose
=
1.25
mg/
L
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
Data
Not
Used
0.0070
Data
Not
Used
0.0220
Data
Not
Used
0.0370
Data
Not
Used
0.0910
$
31,610
0.1800
$
37,514
0.2700
$
38,282
0.3600
$
39,139
0.6800
$
41,955
1.0000
$
39,109
1.2000
$
79,647
2.0000
$
81,086
3.5000
$
185,629
7.0000
$
205,304
17.0000
$
259,851
22.0000
$
287,126
76.0000
$
582,407
210.0000
$
866,583
430.0000
$
1,204,376
520.0000
$
1,323,707
1500.0000
$
2,623,085
Exhibit
D.
5
­
Capital
Costs
for
Chlorine
Dioxide
Capital
Costs
for
Chlorine
Dioxide
(
ClO2
Dose
=
1.25
mg/
L)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
8
June
2003
Constraints:
Not
practical
for
systems
serving
500
or
fewer
people
Design
Criteria:
1)
ClO2
dose
=
1.25
mg/
L
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
Not
Applicable
0.00150
Not
Applicable
0.00540
Not
Applicable
0.00950
Not
Applicable
0.02500
$
14,880
0.05400
$
16,053
0.08400
$
16,826
0.11000
$
17,105
0.23000
$
17,922
0.35000
$
18,685
0.41000
$
19,100
0.77000
$
21,419
1.40000
$
21,327
3.00000
$
24,665
7.80000
$
35,050
11.00000
$
41,359
38.00000
$
85,583
120.00000
$
214,036
270.00000
$
422,373
350.00000
$
533,451
750.00000
$
1,088,846
Exhibit
D.
6
­
O&
M
Costs
for
Chlorine
Dioxide
O&
M
Costs
for
Chlorine
Dioxide
(
ClO2
dose
1.25
mg/
L)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
9
June
2003
Constraints:
None
Design
Criteria:
1)
UV
254
=
0.051
cm­
1,
Turbidity
=
0.1
NTU,
Alkalinity
=
60
mg/
L
CaCO3,
Hardness
=
100
mg/
L
CaCO3
2)
UV
dose
=
40
mJ/
cm2
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
9,924
0.0070
$
9,924
0.0220
$
12,645
0.0370
$
15,329
0.0910
$
24,687
0.1800
$
39,068
0.2700
$
52,290
0.3600
$
64,184
0.6800
$
95,721
1.0000
$
222,584
1.2000
$
233,919
2.0000
$
307,127
3.5000
$
408,427
7.0000
$
660,687
17.0000
$
1,300,376
22.0000
$
1,594,181
76.0000
$
4,642,358
210.0000
$
12,159,564
430.0000
$
25,171,112
520.0000
$
30,742,815
1,500.0000
$
91,412,472
Exhibit
D.
7
­
Capital
Costs
for
UV
(
40
mJ/
cm2)

Capital
Costs
for
UV
(
UV
dose
40
mJ/
cm2,
UV
254
=
0.051
cm­
1,
Turbidity
=
0.1
NTU)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
0.0001
0.0010
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
10,000.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
10
June
2003
Constraints:
None
Design
Criteria:
1)
UV
254
=
0.051
cm­
1,
Turbidity
=
0.1
NTU,
Alkalinity
=
60
mg/
L
CaCO3,
Hardness
=
100
mg/
L
CaCO3
2)
UV
dose
=
40
mJ/
cm2
Average
Flow
O&
M
Cost
(
mgd)
($)
0.0001
$
3,399
0.0015
$
3,399
0.0054
$
3,429
0.0095
$
3,818
0.0250
$
4,579
0.0540
$
4,769
0.0840
$
6,119
0.1100
$
6,498
0.2300
$
8,159
0.3500
$
9,024
0.4100
$
9,457
0.7700
$
11,499
1.4000
$
13,938
3.0000
$
16,140
7.8000
$
22,853
11.0000
$
27,468
38.0000
$
66,624
120.0000
$
187,881
270.0000
$
418,801
350.0000
$
546,773
750.0000
$
1,186,635
Exhibit
D.
8
O&
M
Costs
for
UV
(
40
mJ/
cm2)

O&
M
Costs
for
UV
(
UV
dose
40
mJ/
cm2,
UV
254
=
0.051
cm­
1,
Turbidity
=
0.1
NTU)

$
1,000
$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.0000
0.0001
0.0010
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
11
June
2003
Constraints:
None
Design
Criteria:
1)
UV
254
=
0.051
cm­
1,
Turbidity
=
0.1
NTU
2)
Alkalinity
=
60
mg/
L
CaCO3,
Hardness
=
100
mg/
L
CaCO3
3)
UV
dose
=
200
mJ/
cm2
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
19,937
0.0070
$
19,937
0.0220
$
24,013
0.0370
$
28,088
0.0910
$
42,760
0.1800
$
66,942
0.2700
$
91,395
0.3600
$
115,849
0.6800
$
202,794
1.0000
$
449,368
1.2000
$
489,097
2.0000
$
696,192
3.5000
$
1,003,788
7.0000
$
1,760,142
17.0000
$
3,833,256
22.0000
$
4,663,129
76.0000
$
13,625,666
210.0000
$
35,881,035
430.0000
$
72,395,074
520.0000
$
87,332,636
1,500.0000
$
249,986,083
Exhibit
D.
9
Capital
Costs
for
UV
(
200
mJ/
cm2)

Capital
Costs
for
UV
(
UV
dose
200
mJ/
cm2,
Turbidity
0.1
NTU,

UV254
0.051
cm­
1)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.0001
0.0010
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
10,000.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
12
June
2003
Constraints:
None
Design
Criteria:
1)
UV
254
=
0.051
cm^­
1,
Turbidity
=
0.1
NTU
2)
Alkalinity
=
60
mg/
L
CaCO3,
Hardness
=
100
mg/
L
CaCO3
3)
UV
dose
=
200
mJ/
cm2
Average
Flow
O&
M
Cost
(
mgd)
($)
0.0001
$
3,984
0.0015
$
3,984
0.0054
$
4,118
0.0095
$
4,686
0.0250
$
5,975
0.0540
$
7,206
0.0840
$
8,850
0.1100
$
9,230
0.2300
$
10,775
0.3500
$
11,497
0.4100
$
12,480
0.7700
$
15,392
1.4000
$
19,142
3.0000
$
29,196
7.8000
$
71,152
11.0000
$
99,163
38.0000
$
336,820
120.0000
$
1,072,973
270.0000
$
2,475,577
350.0000
$
3,253,233
750.0000
$
7,141,510
Exhibit
D.
10
­
O&
M
Costs
for
UV
(
200
mJ/
cm2)

O&
M
Costs
for
UV
(
UV
dose
200
mJ/
cm2,
Turbidity
0.1
NTU,

UV254
0.051
cm­
1)

$
1,000
$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.0000
0.0001
0.0010
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
13
June
2003
Constraints:
Not
practical
for
systems
serving
100
or
fewer
people
Design
Criteria:
1)
Contact
time
=
12
minutes
2)
Ozone
maximum
dose
=
3.19
mg/
L
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
Data
Not
Used
0.0070
Data
Not
Used
0.0220
Data
Not
Used
0.0370
Data
Not
Used
0.0910
$
306,733
0.1800
$
331,732
0.2700
$
410,701
0.3600
$
429,873
0.6800
$
574,835
1.0000
$
655,369
1.2000
$
748,729
2.0000
$
1,108,348
3.5000
$
1,400,987
7.0000
$
2,039,310
17.0000
$
3,569,008
22.0000
$
4,057,564
76.0000
$
11,437,951
210.0000
$
23,271,892
430.0000
$
39,346,816
520.0000
$
46,476,447
1500.0000
$
124,110,202
Exhibit
D.
11
­
Capital
Costs
for
Ozone
0.5­
Log
Inactivation
of
Cryptosporidium
Capital
Costs
for
Ozone
0.5­
Log
Inactivation
of
Cryptosporidium
(
Maximum
Dose
=
3.19
mg/
L,
Contact
Time
=
12
minutes)

$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
14
June
2003
Constraints:
Not
practical
for
systems
serving
100
or
fewer
people
Design
Criteria:
1)
Contact
time
=
12
minutes
2)
Ozone
maximum
dose
=
3.19
mg/
L
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
Data
Not
Used
0.00150
Data
Not
Used
0.00540
Data
Not
Used
0.00950
Data
Not
Used
0.02500
$
56,531
0.05400
$
56,686
0.08400
$
57,147
0.11000
$
57,286
0.23000
$
58,379
0.35000
$
59,246
0.41000
$
59,942
0.77000
$
63,369
1.40000
$
70,679
3.00000
$
84,708
7.80000
$
126,345
11.00000
$
151,853
38.00000
$
386,197
120.00000
$
1,131,923
270.00000
$
2,326,749
350.00000
$
2,965,095
750.00000
$
6,156,829
Exhibit
D.
12
­
O&
M
Costs
for
Ozone
0.5­
Log
Inactivation
of
Cryptosporidium
O&
M
Costs
for
Ozone
0.5­
Log
Inactivation
of
Cryptosporidium
(
Average
Dose
=
1.78
mg/
L,
Contact
Time
=
12
minutes)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
15
June
2003
Constraints:
Not
practical
for
systems
serving
100
or
fewer
people
Design
Criteria:
1)
Contact
time
=
12
minutes
2)
Ozone
maximum
dose
=
3.19
mg/
L
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
Data
Not
Used
0.0070
Data
Not
Used
0.0220
Data
Not
Used
0.0370
Data
Not
Used
0.0910
$
306,733
0.1800
$
390,345
0.2700
$
410,701
0.3600
$
517,793
0.6800
$
618,795
1.0000
$
832,071
1.2000
$
984,875
2.0000
$
1,207,059
3.5000
$
1,560,888
7.0000
$
2,527,627
17.0000
$
3,760,584
22.0000
$
4,474,581
76.0000
$
12,835,717
210.0000
$
25,122,969
430.0000
$
45,090,556
520.0000
$
52,943,646
1500.0000
$
138,455,070
Exhibit
D.
13
­
Capital
Costs
for
Ozone
1.0­
Log
Inactivation
of
Cryptosporidium
Capital
Costs
for
Ozone
1.0­
Log
Inactivation
of
Cryptosporidium
(
Maximum
Dose
=
5.00
mg/
L,
Contact
Time
=
12
minutes)

$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
16
June
2003
Constraints:
Not
practical
for
systems
serving
100
or
fewer
people
Design
Criteria:
1)
Contact
time
=
12
minutes
2)
Ozone
maximum
dose
=
3.19
mg/
L
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
Data
Not
Used
0.00150
Data
Not
Used
0.00540
Data
Not
Used
0.00950
Data
Not
Used
0.02500
$
56,652
0.05400
$
57,163
0.08400
$
57,382
0.11000
$
58,021
0.23000
$
59,121
0.35000
$
61,121
0.41000
$
62,308
0.77000
$
65,533
1.40000
$
76,182
3.00000
$
97,490
7.80000
$
152,412
11.00000
$
189,778
38.00000
$
516,761
120.00000
$
1,529,391
270.00000
$
3,232,212
350.00000
$
4,130,989
750.00000
$
8,624,877
Exhibit
D.
14
­
O&
M
Costs
for
Ozone
1.0­
Log
Inactivation
of
Cryptosporidium
O&
M
Costs
for
Ozone
1.0­
Log
Inactivation
of
Cryptosporidium
(
Average
Dose
=
2.75
mg/
L,
Contact
Time
=
12
minutes)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
17
June
2003
Constraints:
Not
practical
for
systems
serving
100
or
fewer
people
Design
Criteria:
1)
Contact
time
=
12
minutes
2)
Ozone
maximum
dose
=
3.19
mg/
L
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
Data
Not
Used
0.0070
Data
Not
Used
0.0220
Data
Not
Used
0.0370
Data
Not
Used
0.0910
$
365,347
0.1800
$
390,345
0.2700
$
498,621
0.3600
$
561,753
0.6800
$
838,596
1.0000
$
951,897
1.2000
$
1,082,080
2.0000
$
1,344,897
3.5000
$
1,784,747
7.0000
$
2,786,864
17.0000
$
4,299,684
22.0000
$
5,176,071
76.0000
$
14,058,615
210.0000
$
27,778,067
430.0000
$
51,856,072
520.0000
$
60,994,144
1500.0000
$
160,497,588
Exhibit
D.
15
­
Capital
Costs
for
Ozone
2.0­
Log
Inactivation
of
Cryptosporidium
Capital
Costs
for
Ozone
2.0­
Log
Inactivation
of
Cryptosporidium
(
Maximum
Dose
=
7.50
mg/
L,
Contact
Time
=
12
minutes)

$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
18
June
2003
Constraints:
Not
practical
for
systems
serving
100
or
fewer
people
Design
Criteria:
1)
Contact
time
=
12
minutes
2)
Ozone
maximum
dose
=
3.19
mg/
L
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
Data
Not
Used
0.00150
Data
Not
Used
0.00540
Data
Not
Used
0.00950
Data
Not
Used
0.02500
$
57,095
0.05400
$
57,373
0.08400
$
58,111
0.11000
$
58,586
0.23000
$
60,864
0.35000
$
62,767
0.41000
$
63,943
0.77000
$
68,152
1.40000
$
75,704
3.00000
$
165,293
7.80000
$
315,611
11.00000
$
399,581
38.00000
$
1,234,372
120.00000
$
3,485,535
270.00000
$
7,215,870
350.00000
$
8,915,410
750.00000
$
17,413,112
Exhibit
D.
16
­
O&
M
Costs
for
Ozone
2.0­
Log
Inactivation
of
Cryptosporidium
O&
M
Costs
for
Ozone
2.0­
Log
Inactivation
of
Cryptosporidium
(
Average
Dose
=
3.91
mg/
L,
Contact
Time
=
12
minutes)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
19
June
2003
Constraints:
None
Design
Criteria:
1)
Water
temp.
10
degrees
C
2)
Sanitary
Sewer
Discharge
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
126,730
0.0070
$
126,730
0.0220
$
206,121
0.0370
$
260,157
0.0910
$
393,517
0.1800
$
605,175
0.2700
$
720,600
0.3600
$
818,777
0.6800
$
1,089,993
1.0000
$
1,533,916
1.2000
$
1,672,053
2.0000
$
2,615,310
3.5000
$
3,981,989
7.0000
$
7,095,991
17.0000
$
15,365,946
22.0000
$
19,274,465
76.0000
$
58,795,535
210.0000
$
147,293,783
430.0000
$
282,503,048
520.0000
$
335,884,024
1500.0000
$
917,143,536
Exhibit
D.
17
­
Capital
Costs
for
Microfiltration/
Ultrafiltration
(
MF/
UF)

Capital
Costs
for
MF/
UF
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.0001
0.001
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
20
June
2003
Constraints:
None
Design
Criteria:
1)
Water
temp.
10
degrees
C
2)
Sanitary
Sewer
Discharge
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
$
7,145
0.0015
$
7,145
0.0054
$
7,601
0.0095
$
8,071
0.0250
$
9,815
0.0540
$
23,306
0.0840
$
26,497
0.1100
$
29,421
0.2300
$
41,671
0.3500
$
69,500
0.4100
$
75,603
0.7700
$
106,304
1.4000
$
162,699
3.0000
$
321,899
7.8000
$
781,382
11.0000
$
1,029,635
38.0000
$
3,295,042
120.0000
$
9,873,367
270.0000
$
21,396,307
350.0000
$
27,162,834
750.0000
$
55,995,468
Exhibit
D.
18
­
O&
M
Costs
for
Microfiltration/
Ultrafiltration
(
MF/
UF)

O&
M
Costs
for
MF/
UF
$
1,000
$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
0.00001
0.0001
0.001
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
21
June
2003
Design
Criteria:
1)
Nominal
pore
size
=
1
micron
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
10,280
0.0070
$
10,280
0.0220
$
10,421
0.0370
$
12,828
0.0910
$
13,320
0.1800
$
19,487
0.2700
$
23,423
0.3600
$
28,771
0.6800
$
42,479
1.0000
$
65,654
1.2000
$
75,011
2.0000
$
136,788
3.5000
Data
Not
Used
7.0000
Data
Not
Used
17.0000
Data
Not
Used
22.0000
Data
Not
Used
76.0000
Data
Not
Used
210.0000
Data
Not
Used
430.0000
Data
Not
Used
520.0000
Data
Not
Used
1500.0000
Data
Not
Used
Exhibit
D.
19
­
Capital
Costs
for
Bag
Filtration
Capital
Costs
for
Bag
Filtration
$
10,000
$
100,000
$
1,000,000
0.0001
0.001
0.01
0.1
1
10
Design
Flow
(
mgd)
Capital
Cost
($)

D­
22
June
2003
Design
Criteria:
1)
Nominal
pore
size
=
1
micron
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
$
527
0.00150
$
527
0.00540
$
529
0.00950
$
750
0.02500
$
758
0.05400
$
992
0.08400
$
1,226
0.11000
$
1,676
0.23000
$
2,605
0.35000
$
3,963
0.41000
$
4,858
0.77000
$
8,119
1.40000
Data
Not
Used
3.00000
Data
Not
Used
7.80000
Data
Not
Used
11.00000
Data
Not
Used
38.00000
Data
Not
Used
120.00000
Data
Not
Used
270.00000
Data
Not
Used
350.00000
Data
Not
Used
1500.00000
Data
Not
Used
Exhibit
D.
20
­
O&
M
Costs
for
Bag
Filtration
O&
M
Costs
for
Bag
Filtration
$
100
$
1,000
$
10,000
0.00001
0.0001
0.001
0.01
0.1
1
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
23
June
2003
Design
Criteria:
1)
Nominal
pore
size
=
1
micron
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
10,465
0.0070
$
10,465
0.0220
$
10,606
0.0370
$
13,197
0.0910
$
17,256
0.1800
$
24,024
0.2700
$
31,480
0.3600
$
43,699
0.6800
$
73,535
1.0000
$
111,151
1.2000
$
136,393
2.0000
$
265,091
3.5000
Data
Not
Used
7.0000
Data
Not
Used
17.0000
Data
Not
Used
22.0000
Data
Not
Used
76.0000
Data
Not
Used
210.0000
Data
Not
Used
430.0000
Data
Not
Used
520.0000
Data
Not
Used
1500.0000
Data
Not
Used
Exhibit
D.
21
­
Capital
Costs
for
Cartridge
Filtration
Capital
Costs
for
Cartridge
Filtration
$
10,000
$
100,000
$
1,000,000
0.0001
0.001
0.01
0.1
1
10
Design
Flow
(
mgd)
Capital
Cost
($)

D­
24
June
2003
Design
Criteria:
1)
Nominal
pore
size
=
1
micron
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
$
725
0.00150
$
725
0.00540
$
727
0.00950
$
1,146
0.02500
$
1,490
0.05400
$
2,836
0.08400
$
4,600
0.11000
$
5,625
0.23000
$
9,826
0.35000
$
14,321
0.41000
$
18,082
0.77000
$
28,157
1.40000
Data
Not
Used
3.00000
Data
Not
Used
7.80000
Data
Not
Used
11.00000
Data
Not
Used
38.00000
Data
Not
Used
120.00000
Data
Not
Used
270.00000
Data
Not
Used
350.00000
Data
Not
Used
1500.00000
Data
Not
Used
Exhibit
D.
22
­
O&
M
Costs
for
Cartrige
Filtration
O&
M
Costs
for
Cartridge
Filtration
$
100
$
1,000
$
10,000
$
100,000
0.00001
0.0001
0.001
0.01
0.1
1
10
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
25
June
2003
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
150,000
0.0070
$
150,000
0.0220
$
150,000
0.0370
$
150,000
0.0910
$
150,000
0.1800
$
150,000
0.2700
$
150,000
0.3600
$
150,000
0.6800
$
150,000
1.0000
$
224,684
1.2000
$
271,361
2.0000
$
458,070
3.5000
$
808,149
7.0000
$
1,625,000
17.0000
$
3,382,246
22.0000
$
4,260,870
76.0000
$
13,750,000
210.0000
$
37,297,101
430.0000
$
75,956,522
520.0000
$
91,771,739
1500.0000
$
263,981,884
Exhibit
D.
23
­
Capital
Costs
for
Bank
Filtration
Capital
Costs
for
Bank
Filtration
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.0001
0.001
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
26
June
2003
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
1,106,000
0.0070
$
1,106,000
0.0220
$
1,106,000
0.0370
$
1,106,000
0.0910
$
1,106,000
0.1800
$
1,106,000
0.2700
$
1,106,000
0.3600
$
1,106,000
0.6800
$
1,106,000
1.0000
$
1,331,013
1.2000
$
1,471,646
2.0000
$
2,034,177
3.5000
$
3,088,924
7.0000
$
5,550,000
17.0000
$
7,731,159
22.0000
$
8,821,739
76.0000
$
20,600,000
210.0000
$
49,827,536
430.0000
$
97,813,043
520.0000
$
117,443,478
1500.0000
$
331,197,101
Exhibit
D.
24
­
Capital
Costs
for
Secondary
Filters
Capital
Costs
for
Secondary
Filters
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.0001
0.001
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
27
June
2003
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
$
62,300
0.00150
$
62,300
0.00540
$
62,300
0.00950
$
62,300
0.02500
$
62,300
0.05400
$
62,300
0.08400
$
62,300
0.11000
$
62,300
0.23000
$
62,300
0.35000
$
66,034
0.41000
$
67,901
0.77000
$
79,104
1.40000
$
98,709
3.00000
$
148,500
7.80000
$
182,031
11.00000
$
204,386
38.00000
$
393,000
120.00000
$
965,829
270.00000
$
2,013,686
350.00000
$
2,572,543
750.00000
$
5,366,829
Exhibit
D.
25
­
O&
M
Costs
for
Secondary
Filters
O&
M
Costs
for
Secondary
Filters
$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.00001
0.0001
0.001
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
28
June
2003
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
1,200,000
0.0070
$
1,200,000
0.0220
$
1,200,000
0.0370
$
1,200,000
0.0910
$
1,200,000
0.1800
$
1,200,000
0.2700
$
1,200,000
0.3600
$
1,200,000
0.6800
$
1,200,000
1.0000
$
1,326,582
1.2000
$
1,405,696
2.0000
$
1,722,152
3.5000
$
2,315,506
7.0000
$
3,700,000
17.0000
$
6,859,420
22.0000
$
8,439,130
76.0000
$
25,500,000
210.0000
$
67,836,232
430.0000
$
137,343,478
520.0000
$
165,778,261
1500.0000
$
475,401,449
Exhibit
D.
26
­
Capital
Costs
for
Pre­
sedimentation
with
Coagulant
Capital
Costs
for
Pre­
sedimentation
with
Coagulant
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.0001
0.001
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
29
June
2003
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
$
37,000
0.00150
$
37,000
0.00540
$
37,000
0.00950
$
37,000
0.02500
$
37,000
0.05400
$
37,000
0.08400
$
37,000
0.11000
$
37,000
0.23000
$
37,000
0.35000
$
40,552
0.41000
$
42,329
0.77000
$
52,986
1.40000
$
71,635
3.00000
$
119,000
7.80000
$
179,480
11.00000
$
219,800
38.00000
$
560,000
120.00000
$
1,593,200
270.00000
$
3,483,200
350.00000
$
4,491,200
750.00000
$
9,531,200
Exhibit
D.
27
­
O&
M
Costs
for
Pre­
sedimentation
with
Coagulant
O&
M
Costs
for
Pre­
sedimentation
with
Coagulant
$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.00001
0.0001
0.001
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
30
June
2003
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
250,000
0.0070
$
250,000
0.0220
$
250,000
0.0370
$
250,000
0.0910
$
250,000
0.1800
$
250,000
0.2700
$
250,000
0.3600
$
250,000
0.6800
$
250,000
1.0000
$
262,658
1.2000
$
270,570
2.0000
$
302,215
3.5000
$
361,551
7.0000
$
500,000
17.0000
$
572,464
22.0000
$
608,696
76.0000
$
1,000,000
210.0000
$
1,971,014
430.0000
$
3,565,217
520.0000
$
4,217,391
1500.0000
$
11,318,841
Exhibit
D.
28
­
Capital
Costs
for
Watershed
Control
Capital
Costs
for
Watershed
Control
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
0.0001
0.001
0.01
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
31
June
2003
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
$
350,000
0.00150
$
350,000
0.00540
$
350,000
0.00950
$
350,000
0.02500
$
350,000
0.05400
$
350,000
0.08400
$
350,000
0.11000
$
350,000
0.23000
$
350,000
0.35000
$
378,159
0.41000
$
392,238
0.77000
$
476,715
1.40000
$
624,549
3.00000
$
1,000,000
7.80000
$
1,205,714
11.00000
$
1,342,857
38.00000
$
2,500,000
120.00000
$
6,014,286
270.00000
$
12,442,857
350.00000
$
15,871,429
750.00000
$
33,014,286
Exhibit
D.
29
­
O&
M
Costs
for
Watershed
Control
O&
M
Costs
for
Watershed
Control
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
0.00001
0.0001
0.001
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
32
June
2003
Constraints:
Not
practical
for
systems
serving
fewer
than
500
people
Design
Criteria:
1)
See
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
ch.
3.3.11
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
Not
Applicable
0.0070
Not
Applicable
0.0220
Not
Applicable
0.0370
Not
Applicable
0.0910
Not
Applicable
0.1800
$
9,986
0.2700
$
17,840
0.3600
$
19,764
0.6800
$
24,486
1.0000
$
30,133
1.2000
$
33,186
2.0000
$
42,497
3.5000
$
58,321
7.0000
$
90,156
17.0000
$
136,850
22.0000
$
150,119
76.0000
$
653,715
210.0000
$
1,069,457
430.0000
$
1,759,746
520.0000
$
2,215,996
1500.0000
$
7,184,046
Exhibit
D.
30
­
Capital
Costs
for
Combined
Filter
Performance
Capital
Costs
for
Combined
Filter
Performance
$
10,000
$
100,000
$
1,000,000
$
10,000,000
0.1
1
10
100
1000
10000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
33
June
2003
Constraints:
Not
practical
for
systems
serving
fewer
than
500
people
Design
Criteria:
1)
See
Technologies
and
Costs
for
Control
of
Microbial
Contaminants
and
Disinfection
Byproducts
ch.
3.3.11
Average
Flow
O&
M
Cost
(
mgd)
($)
0.00005
Not
Applicable
0.00150
Not
Applicable
0.00540
Not
Applicable
0.00950
Not
Applicable
0.02500
Not
Applicable
0.05400
$
7,090
0.08400
$
16,626
0.11000
$
16,698
0.23000
$
17,295
0.35000
$
20,227
0.41000
$
21,986
0.77000
$
31,954
1.40000
$
33,036
3.00000
$
35,702
7.80000
$
58,854
11.00000
$
65,124
38.00000
$
133,775
120.00000
$
161,628
270.00000
$
212,517
350.00000
$
225,069
750.00000
$
287,831
Exhibit
D.
31
­
O&
M
Costs
for
Combined
Filter
Performance
O&
M
Costs
for
Combined
Filter
Performance
$
1,000
$
10,000
$
100,000
$
1,000,000
0.01
0.1
1
10
100
1000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
34
June
2003
Constraints:
Not
practical
for
systems
serving
10,000
or
fewer
people
Design
Criteria:
1)
Reactivation
frequency
=
360
days
2)
Onsite
generation
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
Not
Applicable
0.0070
Not
Applicable
0.0220
Not
Applicable
0.0370
$
60,750
0.0910
$
97,307
0.1800
$
153,426
0.2700
$
206,628
0.3600
$
258,604
0.6800
$
434,477
1.0000
$
753,229
1.2000
$
961,218
2.0000
$
1,331,550
3.5000
$
1,935,301
7.0000
$
3,129,311
17.0000
$
5,894,486
22.0000
$
7,103,058
76.0000
$
17,577,650
210.0000
$
36,661,251
430.0000
$
61,958,498
520.0000
$
71,251,757
1,500.0000
$
172,445,012
Exhibit
D.
32
­
Capital
Costs
for
GAC10
Surface
Water
Plants
Capital
Costs
for
GAC10
(
Reactivation
frequency
360
days,
onsite
regeneration)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
10,000.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
35
June
2003
Constraints:
Not
practical
for
systems
serving
10,000
or
fewer
people
Design
Criteria:
1)
Reactivation
frequency
=
360
days
2)
Onsite
generation
Average
Flow
O&
M
Cost
(
mgd)
($)
0.0001
Not
Applicable
0.0015
Not
Applicable
0.0054
Not
Applicable
0.0095
$
12,360
0.0250
$
19,485
0.0540
$
28,052
0.0840
$
30,902
0.1100
$
34,917
0.2300
$
46,132
0.3500
$
57,232
0.4100
$
51,976
0.7700
$
61,522
1.4000
$
77,734
3.0000
$
117,714
7.8000
$
223,726
11.0000
$
276,141
38.0000
$
700,590
120.0000
$
1,930,628
270.0000
$
4,109,268
350.0000
$
5,253,236
750.0000
$
10,973,076
Exhibit
D.
33
­
O&
M
Costs
for
GAC10
Surface
Water
Plants
O&
M
Costs
for
GAC10
(
Reactivation
frequency
360
days,
onsite
regeneration)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
­
100.0000
200.0000
300.0000
400.0000
500.0000
600.0000
700.0000
800.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
36
June
2003
Constraints:
None
Design
Criteria:
1)
Reactivation
frequency
=
90
days
2)
Onsite
generation
for
systems
serving
more
than
10,000
people
3)
Media
replacement
for
systems
serving
10,000
or
fewer
people
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
34,944
0.0070
$
34,944
0.0220
$
51,211
0.0370
$
67,885
0.0910
$
132,410
0.1800
$
232,148
0.2700
$
326,766
0.3600
$
417,447
0.6800
$
708,992
1.0000
$
1,179,491
1.2000
$
1,491,296
2.0000
$
2,117,739
3.5000
$
3,146,100
7.0000
$
5,196,469
17.0000
$
9,994,133
22.0000
$
12,105,188
76.0000
$
30,250,612
210.0000
$
64,392,745
430.0000
$
110,161,213
520.0000
$
127,064,791
1,500.0000
$
311,125,976
Exhibit
D.
34
­
Capital
Costs
for
GAC20
Surface
Water
Plants
Capital
Costs
for
GAC20
(
Reactivation
frequency
90
days)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
­
200.0000
400.0000
600.0000
800.0000
1,000.0000
1,200.0000
1,400.0000
1,600.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
37
June
2003
Constraints:
None
Design
Criteria:
1)
Reactivation
frequency
=
90
days
2)
Onsite
generation
for
systems
serving
more
than
10,000
people
3)
Media
replacement
for
systems
serving
10,000
or
fewer
people
Average
Flow
O&
M
Cost
(
mgd)
($)
0.0001
$
9,222
0.0015
$
9,222
0.0054
$
18,223
0.0095
$
25,644
0.0250
$
47,782
0.0540
$
48,603
0.0840
$
61,851
0.1100
$
74,549
0.2300
$
123,862
0.3500
$
171,361
0.4100
$
177,461
0.7700
$
198,999
1.4000
$
235,875
3.0000
$
327,328
7.8000
$
649,586
11.0000
$
854,448
38.0000
$
2,426,385
120.0000
$
6,675,323
270.0000
$
13,806,859
350.0000
$
17,448,504
750.0000
$
35,656,731
Exhibit
D.
35
­
O&
M
Costs
for
GAC20
Surface
Water
Plants
O&
M
Costs
for
GAC20
(
Reactivation
frequency
90
days)

$
1,000
$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
­
100.0000
200.0000
300.0000
400.0000
500.0000
600.0000
700.0000
800.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
38
June
2003
Constraints:
None
Design
Criteria:
1)
Reactivation
frequency
=
240
days
2)
Onsite
regeneration
for
systems
serving
more
than
10,000
people
3)
Media
replacement
for
systems
serving
10,000
or
fewer
people
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
34,944
0.0070
$
34,944
0.0220
$
51,211
0.0370
$
67,885
0.0910
$
132,410
0.1800
$
232,148
0.2700
$
326,766
0.3600
$
417,447
0.6800
$
708,992
1.0000
$
1,179,491
1.2000
$
1,299,190
2.0000
$
1,855,588
3.5000
$
2,780,301
7.0000
$
4,651,079
17.0000
$
9,110,253
22.0000
$
11,096,119
76.0000
$
28,529,679
210.0000
$
62,098,782
430.0000
$
107,964,358
520.0000
$
125,068,321
1,500.0000
$
311,311,471
Exhibit
D.
36
­
Capital
Costs
for
GAC20
Ground
Water
Plants
Capital
costs
for
GAC20
(
Reactivation
frequency
240
days)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
0.0001
0.0010
0.0100
0.1000
1.0000
10.0000
100.0000
1,000.0000
10,000.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
39
June
2003
Constraints:
None
Design
Criteria:
1)
Reactivation
frequency
=
240
days
2)
Onsite
regeneration
for
systems
serving
more
than
10,000
people
3)
Media
replacement
for
systems
serving
10,000
or
fewer
people
Average
Flow
O&
M
Cost
(
mgd)
($)
0.0001
$
6,673
0.0015
$
6,673
0.0054
$
11,206
0.0095
$
14,742
0.0250
$
24,752
0.0540
$
36,031
0.0840
$
42,959
0.1100
$
50,255
0.2300
$
75,195
0.3500
$
98,890
0.4100
$
96,841
0.7700
$
110,105
1.4000
$
133,014
3.0000
$
190,387
7.8000
$
361,906
11.0000
$
463,435
38.0000
$
1,278,749
120.0000
$
3,580,415
270.0000
$
7,445,710
350.0000
$
9,260,140
750.0000
$
18,332,287
Exhibit
D.
37
­
O&
M
Costs
for
GAC20
Ground
Water
Plants
O&
M
Costs
for
GAC20
(
Reactivation
frequency
240
days)

$
1,000
$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
­
100.0000
200.0000
300.0000
400.0000
500.0000
600.0000
700.0000
800.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
40
June
2003
Constraints:
None
Design
Criteria:
1)
Water
temp.
10
degrees
C
2)
Ocean
discharge
Design
Flow
Capital
Cost
(
mgd)
($)
0.0001
$
57,525
0.0070
$
57,525
0.0220
$
74,149
0.0370
$
90,772
0.0910
$
157,393
0.1800
$
221,934
0.2700
$
311,361
0.3600
$
351,040
0.6800
$
645,274
1.0000
$
889,719
1.2000
$
1,051,390
2.0000
$
1,954,756
3.5000
$
3,286,990
7.0000
$
6,499,205
17.0000
$
14,869,801
22.0000
$
19,105,695
76.0000
$
55,387,959
210.0000
$
124,824,207
430.0000
$
255,424,078
520.0000
$
306,978,901
1,500.0000
$
868,353,635
Exhibit
D.
38
­
Capital
Costs
for
Nanofiltration
Surface
Water
Plants
Capital
Costs
for
Nanofiltration
(
Temp.
10
degrees
C)

$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
­
200.0000
400.0000
600.0000
800.0000
1,000.0000
1,200.0000
1,400.0000
1,600.0000
Design
Flow
(
mgd)
Capital
Cost
($)

D­
41
June
2003
Constraints:
None
Design
Criteria:
1)
Water
temp.
10
degrees
C
2)
Ocean
discharge
Average
Flow
O&
M
Cost
(
mgd)
($)
0.0001
$
7,789
0.0015
$
7,789
0.0054
$
8,800
0.0095
$
9,872
0.0250
$
14,051
0.0540
$
30,613
0.0840
$
37,777
0.1100
$
43,061
0.2300
$
70,281
0.3500
$
111,819
0.4100
$
125,926
0.7700
$
203,795
1.4000
$
339,238
3.0000
$
703,226
7.8000
$
1,763,644
11.0000
$
2,409,108
38.0000
$
7,862,441
120.0000
$
23,730,069
270.0000
$
52,646,948
350.0000
$
67,712,655
750.0000
$
143,041,188
Exhibit
D.
39
­
O&
M
Costs
for
Nanofiltration
Surface
Water
Plants
O&
M
Costs
for
Nanofiltration
(
Temp.
10
degrees
C)

$
1,000
$
10,000
$
100,000
$
1,000,000
$
10,000,000
$
100,000,000
$
1,000,000,000
­
100.0000
200.0000
300.0000
400.0000
500.0000
600.0000
700.0000
800.0000
Average
Flow
(
mgd)
O&
M
Cost
($)

D­
42
June
2003
