ALL
UNITS
CONTROLLED
SEPARATELY
­
Waste
coals
at
0.38
lb
Hg/
TBtu
Estimated
Inremental
Hg
Impacts
for
Utility
Boilers
Unit
type
Capital
cost,
1999$
Annual
cost,
1999
$/
y
Energy
usage,
kWh/
y
Solid
waste,
tons/
y
Mercury,
tons/
y
Mercury,
tons/
y
Water
usage,
gal/
y
good
units
under
limit
all
units
at
limit
Bituminous
4,609,152,119
727,526,410
89,302,328
193,590
14.44
13.32
207,502,000
Subbituminous
606,731,103
91,932,830
3,938,424
9,423
2.0
­
1.6
0
Lignite
60,739,476
9,471,505
355,016
1,022
0.37
­
0.53
0
Blends
657,368,724
101,378,344
4,545,687
8,510
2.11
1.64
0
IGCC
0
0
0
0
0.00
0
0
Coal
refuse
57,356,198
18,006,389
33,237,538
81,995
0.07
0.05
117,309,435
Total
5,991,347,619
948,315,477
131,378,993
294,540
19
13
324,811,435
Estimated
Inremental
Hg
Impacts
for
Utility
Boilers
Unit
type
Capital
cost,
1999
$
Annual
cost,
1999
$/
y
Energy
usage,
kWh/
y
Solid
waste,
tons/
y
Mercury,
tons/
y
Mercury,
tons/
y
Water
usage,
gal/
y
good
units
under
limit
all
units
at
limit
Bituminous
4,609,000,000
728,000,000
89,300,000
194,000
14.4
13.3
207,502,000
Subbituminous
607,000,000
92,000,000
3,940,000
9,400
2.0
­
1.6
0
Lignite
61,000,000
9,000,000
0
1,000
0.4
­
0.5
0
Blends
657,000,000
101,000,000
4,550,000
8,500
2.1
1.6
0
IGCC
0
0
0
0
0.0
0.0
0
Coal
refuse
57,000,000
18,000,000
33,200,000
82,000
0.1
0.05
117,309,435
Total
5,991,000,000
948,000,000
131,000,000
295,000
19.0
12.9
324,811,435
Estimated
Inremental
Hg
Impacts
for
Utility
Boilers,
Rounded,
in
Milllions
Except
for
Mercury
Unit
type
Capital
cost,
1999
$
Annual
cost,
1999
$/
y
Energy
usage,
kWh/
y
Solid
waste,
tons/
y
Mercury,
tons/
y
Mercury,
tons/
y
Water
usage,
gal/
y
good
units
under
limit
all
units
at
limit
Bituminous
4,609
728
89
0.194
14.4
13.3
208
Subbituminous
607
92
4
0.009
2.0
­
1.6
0
Lignite
61
9
0
0.001
0.4
­
0.5
0
Blends
657
101
5
0.009
2.1
1.6
0
IGCC
0
0
0
0
0.0
0.0
0
Coal
refuse
57
18
33
0.082
0.1
0.05
117
Total
5,991
948
131
0.300
19.0
12.9
325
dwcgi­
5273­
1075236571­
666710000.
xls,
Costs­
impacts
1/
28/
04
Baghouse
costs
and
impacts
equations
based
on
MW
Bituminous
Capital
cost,
1999$/
MWAnnual
cost,
1999
$/
y­
MEnergy
usage,
kWh/
y
Solid
waste
generation,
100
MW
8847*
LN(
M8)+
14386
1295.5*
Ln(
m8)
+
2638.(­
56.224*
LN(
500)+
791..
725*
m8
500
MW
975
MW
Subbituminous
100
MW
8256.1*
Ln(
m555)
+
203.2078x
+
9106.6
­
58.806Ln(
x)
+
828.25
1.112*
m8
500
MW
975
MW
Lignite
100
MW
8047.5Ln(
x)
+
27528
1233Ln(
x)
+
4430.7
­
58.806Ln(
x)
+
828.25
1.317*
m8
500
MW
975
MW
SDA
Capital
cost,
$
Annual
cost,
$/
MW­
y
bit
9.8504*(
m8)
+
168263­
28000
44360
sub
9.8504x
+
168263
41500
lignite
9.8504x
+
168263+
45000
48000
n,
tons/
y
MW
Capital,
$/
MWMW
Annual,
$/
y­
MMW
Energy,
KWh/
y­
MW
100
55,365
100
8,522
100
539
100
500
68,557
500
10,499
500
420
500
975
75,847
975
11,506
975
420
975
100
58,888
100
9,113
100
564
100
500
70,867
500
10,946
500
440
500
975
78,108
975
11,949
975
440
975
100
64,889
100
10,012
100
625
100
500
76,516
500
11,860
500
487
500
975
83,638
975
12,851
975
487
975
Capital
costs,
bituminous,
$/
MW
y
=
8847Ln(
x)
+
14386
R2
=
0.9952
0
20,000
40,000
60,000
80,000
0
500
1000
1500
Unit
size,
Mw
Capital
cost,

1999
$/
MW
Annual
cost,
bituminous,
$/
y­
MW
y
=
1295.3Ln(
x)
+
2532.4
R2
=
0.9976
0
5,000
10,000
15,000
0
500
1,000
1,500
Unit
size,
MW
Annual
cost,

1999
$/
y­
MW
Energy
usage,
bituminous,
kWh/
y
0
200
400
600
nergy
usage,

kWh/
y
Capital
costs
y
=
8256.1Ln(
x)
+
20570
R2
=
0.9914
0
50,000
100,000
0
Capital
cost,

1999
$/
MW
Annual
costs,

y
=
3.2053x
+
8986.6
R2
=
0.9536
0
5,000
10,000
15,000
0
Annual
cost,

1999
$/
y­
MW
Energy
usage
0
200
400
600
nergy
usage,

kWh/
y
Power,
kWh/
y­
MW
Water,
gal/
y­
MW
solid
waste,
ton/
y­
MW
­
above
fly
ash
81,883
289,000
202
89,321
359,834
111
93,500
414,375
149
y
=
­
56.224Ln(
x)
+
791.88
R2
=
0.9186
0
200
0
500
1,000
1,500
Unit
size,
MW
Energy
kW
Solid
waste
generation,
bituminous,
tons/
y
0.725
0.725
0.725
0.725
0.725
0
200
400
600
800
1,000
1,200
Unit
size,
MW
Solid
waste
generation,

tons/
y
y
=
­
58.806Ln(
x)
+
828.25
R2
=
0.9186
0
200
0
Energy
kW
Solid
waste
ge
1.112
1.112
1.112
1.112
1.112
0
200
Solid
waste
generated,

tons/
y
Solid
waste,
tons/
yr­
MW
0.725
0.725
0.725
1.112
1.112
1.112
1.317
1.317
1.317
osts,
subbituminous,
$/
MW
570
500
1000
1500
Unit
size,
MW
sts,
subbituminous,
$/
y­
MW
500
1,000
1,500
Unit
size,
MW
age,
subbituminous,
tons/
y
Capital
cost,
lignite,
$/
MW
y
=
8047.5Ln(
x)
+
27528
R2
=
0.9907
0
50,000
100,000
0
500
1000
1500
Unit
size,
MW
Capital
cost,

1999
$/
y­
MW
Annual
cost,
lignite,
$/
y­
MW
y
=
1228.7Ln(
x)
+
4324.2
R2
=
0.9962
0
5,000
10,000
15,000
0
500
1,000
1,500
Unit
size,
MW
Annual
cost,

1999
$/
y­
MW
Energy
usage,
lignite,
kWh/
y
200
400
600
800
nergy
usage,

kWh/
y
28.25
500
1,000
1,500
Unit
size,
MW
e
generation,
subbituminous,
tons/
y
400
600
800
1,000
1,200
Unit
size,
MW
y
=
­
65.123Ln(
x)
+
917.22
R2
=
0.9186
0
200
400
0
500
1,000
1,500
Unit
size,
MW
Energy
kW
Solid
waste
generation,
lignite,
tons/
y
1.317
1.317
1.317
1.317
0
500
1,000
1,500
Unit
size,
MW
Solid
waste
generation,

tons/
y
1500
1,500
1,500
ns/
y
1,500
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
975
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
880,830
acfm
Collection
rate,
pounds
per
hour
20,960
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
2.78
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
407,791.55
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
880,830
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
2.78
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
3.90
to
1
Calculated
Cloth
Area:
225,986
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
2.16
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
407,792
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
2,750,010
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,359,709
(
4K<
area<
16K)
Insulation
Add­
on
$
185,381
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
3,082,037
(
4K<
area<
60K)
Stainless
steel
add­
on
$
1,940,800
(
20K<
area
<
60K
Insulation
add­
on
$
136,610
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
2,273,747
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,862,270
(
4K<
area<
16K)
Insulation
add­
on
$
381,082
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
3,636,768
(
4K<
area<
24K)
Stainless
steel
add­
on
$
1,733,931
(
4K<
area<
24K)
Insulation
add­
on
$
1,118,377
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
1,912,950
(
10K<
area<
115
Stainless
steel
add­
on
$
842,619
(
10K<
area<
115
Insulation
add­
on
$
375,496
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
2,862,805
(
75K<
area<
550
Stainless
steel
add­
on
$
877,617
(
75K<
area<
550
Insulation
add­
on
$
314,107
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
3,176,912
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.01
$/
square
foot
Calculated
Bag
Cost:
$
411,869
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
2,509,015
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
6,097,796
Instrumentation
$
609,780
Sales
Taxes
$
182,934
Freight
$
304,890
Purchased
Equipment
Cost,
PEC
$
7,195,399
Direct
Installation
Costs
Foundations
and
supports
$
287,816
Handling
and
erection
$
3,597,700
Electrical
$
575,632
Piping
$
71,954
Insulation
for
ductwork
$
503,678
Painting
$
143,908
Direct
Installation
Costs
$
5,180,687
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
12,376,087
Indirect
Costs
(
installation)
Engineering
$
719,540
Construction
and
Field
Expense
$
1,439,080
Contractor
Fees
$
719,540
Start­
up
$
71,954
Performance
Test
$
71,954
Contingencies
$
215,862
Total
Indirect
Costs,
IC
$
3,237,930
TOTAL
CAPITAL
INVESTMENT,
TCI
$
81,547,450
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
81,547,450
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
154,426
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
7,123
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
78,036
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
273,889
Shaker
$
392,600
Pulse­
jet
$
399,815
Enter
appropriate
DC
$
399,815
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
1,630,949
Property
taxes
TCI
*
0.01
$
815,475
Insurance
TCI
*
0.01
$
815,475
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
7,648,128
Total
Indirect
Costs,
IC
$
10,930,608
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
12,529,868
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
lignite
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
$
7,379.90
$
23.15
$/
acfm
$
83.64
$/
kW
Cost
quadrupled
for
4
baghouses,
less
7
%
118,712
kWh
for
one
of
four
baghouses
$
125,926
321
tons
solid
waste
for
one
of
four
baghouses
Set
for
auto
$
14.23
$/
acfm
$
12.85
$/
kW
Direct
cost
quadrupled
for
4
baghouses
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
500
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
903,415
acfm
Collection
rate,
pounds
per
hour
21,498
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
2.78
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
418,247.75
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
903,415
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
2.78
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
3.90
to
1
Calculated
Cloth
Area:
231,781
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
2.16
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
418,248
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
2,820,433
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,394,277
(
4K<
area<
16K)
Insulation
Add­
on
$
190,086
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
3,160,103
(
4K<
area<
60K)
Stainless
steel
add­
on
$
1,989,933
(
20K<
area
<
60K
Insulation
add­
on
$
140,113
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
2,331,799
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,909,752
(
4K<
area<
16K)
Insulation
add­
on
$
390,817
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
3,729,671
(
4K<
area<
24K)
Stainless
steel
add­
on
$
1,778,391
(
4K<
area<
24K)
Insulation
add­
on
$
1,147,059
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
1,961,289
(
10K<
area<
115
Stainless
steel
add­
on
$
863,552
(
10K<
area<
115
Insulation
add­
on
$
384,790
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
2,924,946
(
75K<
area<
550
Stainless
steel
add­
on
$
897,233
(
75K<
area<
550
Insulation
add­
on
$
320,557
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
3,245,503
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.01
$/
square
foot
Calculated
Bag
Cost:
$
422,430
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
1,933,201
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
5,601,135
Instrumentation
$
560,113
Sales
Taxes
$
168,034
Freight
$
280,057
Purchased
Equipment
Cost,
PEC
$
6,609,339
Direct
Installation
Costs
Foundations
and
supports
$
264,374
Handling
and
erection
$
3,304,670
Electrical
$
528,747
Piping
$
66,093
Insulation
for
ductwork
$
462,654
Painting
$
132,187
Direct
Installation
Costs
$
4,758,724
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
11,368,064
Indirect
Costs
(
installation)
Engineering
$
660,934
Construction
and
Field
Expense
$
1,321,868
Contractor
Fees
$
660,934
Start­
up
$
66,093
Performance
Test
$
66,093
Contingencies
$
198,280
Total
Indirect
Costs,
IC
$
2,974,203
TOTAL
CAPITAL
INVESTMENT,
TCI
$
38,258,170
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
38,258,170
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
158,386
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
7,305
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
80,037
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
280,032
Shaker
$
280,032
Pulse­
jet
$
409,187
Enter
appropriate
DC
$
409,187
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
765,163
Property
taxes
TCI
*
0.01
$
382,582
Insurance
TCI
*
0.01
$
382,582
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
3,560,660
Total
Indirect
Costs,
IC
$
5,111,569
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
5,929,943
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
lignite
half
volume
for
2
baghouses
half
volume
for
2
baghouses
half
volume
for
2
baghouses
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
half
volume
for
2
baghouses
half
volume
for
2
baghouses
half
volume
for
2
baghouses
$
13,218.68
$
21.17
$/
acfm
$
76.52
$/
kW
Cost
doubled
for
2
baghouses,
less
5
%
121,756
kWh
$
129,155
329
tons
solid
waste
Set
for
auto
$
6.56
$/
acfm
$
11.86
$/
kW
Direct
cost
doubled
for
2
baghouses
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
100
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
361,366
acfm
Collection
rate,
pounds
per
hour
8,599
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
2.78
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
167,299.10
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
361,366
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
2.78
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
3.90
to
1
Calculated
Cloth
Area:
92,712
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
4.00
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
92,712
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
627,951
(
4K<
area<
16K)
Stainless
steel
add­
on
$
318,057
(
4K<
area<
16K)
Insulation
Add­
on
$
43,596
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
729,655
(
4K<
area<
60K)
Stainless
steel
add­
on
$
460,242
(
20K<
area
<
60K
Insulation
add­
on
$
31,059
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
524,427
(
4K<
area<
16K)
Stainless
steel
add­
on
$
431,496
(
4K<
area<
16K)
Insulation
add­
on
$
87,743
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
837,289
(
4K<
area<
24K)
Stainless
steel
add­
on
$
394,214
(
4K<
area<
24K)
Insulation
add­
on
$
254,115
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
456,339
(
10K<
area<
115
Stainless
steel
add­
on
$
211,830
(
10K<
area<
115
Insulation
add­
on
$
95,422
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
990,289
(
75K<
area<
550
Stainless
steel
add­
on
$
286,528
(
75K<
area<
550
Insulation
add­
on
$
119,734
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
1,091,404
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.60
$/
square
foot
Calculated
Bag
Cost:
$
150,022
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
563,561
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
1,804,987
Instrumentation
$
180,499
Sales
Taxes
$
54,150
Freight
$
90,249
Purchased
Equipment
Cost,
PEC
$
2,129,885
Direct
Installation
Costs
Foundations
and
supports
$
85,195
Handling
and
erection
$
1,064,942
Electrical
$
170,391
Piping
$
21,299
Insulation
for
ductwork
$
149,092
Painting
$
42,598
Direct
Installation
Costs
$
1,533,517
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
3,663,402
Indirect
Costs
(
installation)
Engineering
$
212,988
Construction
and
Field
Expense
$
425,977
Contractor
Fees
$
212,988
Start­
up
$
21,299
Performance
Test
$
21,299
Contingencies
$
63,897
Total
Indirect
Costs,
IC
$
958,448
TOTAL
CAPITAL
INVESTMENT,
TCI
$
6,488,864
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
6,488,864
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
56,249
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
2,922
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
32,015
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
125,490
Shaker
$
125,490
Pulse­
jet
$
126,523
Enter
appropriate
DC
$
126,523
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
129,777
Property
taxes
TCI
*
0.01
$
64,889
Insurance
TCI
*
0.01
$
64,889
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
594,518
Total
Indirect
Costs,
IC
$
874,655
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
1,001,179
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
lignite
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
$
21,298.85
$
17.96
$/
acfm
$
64.89
$/
kW
62,479
kWh
$
1,033
132
tons
solid
waste
Set
for
auto
$
2.77
$/
acfm
10.01
$/
MW
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
975
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
795,391
acfm
Collection
rate,
pounds
per
hour
17,699
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
2.60
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
368,236.48
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
795,391
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
2.60
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
3.91
to
1
Calculated
Cloth
Area:
203,243
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
2.16
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
368,236
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
2,483,607
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,228,940
(
4K<
area<
16K)
Insulation
Add­
on
$
167,581
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
2,786,719
(
4K<
area<
60K)
Stainless
steel
add­
on
$
1,754,930
(
20K<
area
<
60K
Insulation
add­
on
$
123,359
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
2,054,137
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,682,651
(
4K<
area<
16K)
Insulation
add­
on
$
344,256
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
3,285,321
(
4K<
area<
24K)
Stainless
steel
add­
on
$
1,565,743
(
4K<
area<
24K)
Insulation
add­
on
$
1,009,878
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
1,730,087
(
10K<
area<
115
Stainless
steel
add­
on
$
763,429
(
10K<
area<
115
Insulation
add­
on
$
340,335
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
2,627,729
(
75K<
area<
550
Stainless
steel
add­
on
$
803,412
(
75K<
area<
550
Insulation
add­
on
$
289,705
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
2,917,434
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.01
$/
square
foot
Calculated
Bag
Cost:
$
371,919
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
2,405,224
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
5,694,577
Instrumentation
$
569,458
Sales
Taxes
$
170,837
Freight
$
284,729
Purchased
Equipment
Cost,
PEC
$
6,719,601
Direct
Installation
Costs
Foundations
and
supports
$
268,784
Handling
and
erection
$
3,359,801
Electrical
$
537,568
Piping
$
67,196
Insulation
for
ductwork
$
470,372
Painting
$
134,392
Direct
Installation
Costs
$
4,838,113
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
11,557,714
Indirect
Costs
(
installation)
Engineering
$
671,960
Construction
and
Field
Expense
$
1,343,920
Contractor
Fees
$
671,960
Start­
up
$
67,196
Performance
Test
$
67,196
Contingencies
$
201,588
Total
Indirect
Costs,
IC
$
3,023,820
TOTAL
CAPITAL
INVESTMENT,
TCI
$
76,155,097
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
76,155,097
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
139,447
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
6,432
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
65,894
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
246,077
Shaker
$
353,274
Pulse­
jet
$
359,788
Enter
appropriate
DC
$
359,788
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
1,523,102
Property
taxes
TCI
*
0.01
$
761,551
Insurance
TCI
*
0.01
$
761,551
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
7,143,917
Total
Indirect
Costs,
IC
$
10,210,703
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
11,649,857
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
subbituminous
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
$
23.94
$/
acfm
$
78.11
$/
kW
Cost
quadrupled
for
4
baghouses,
less
7
%
107,197
kWh
$
113,712
271
tons
solid
waste
Set
for
auto
$
14.65
$/
acfm
$
11.95
$/
kW
Direct
cost
quadrupled
for
4
baghouses
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
500
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
815,785
acfm
Collection
rate,
pounds
per
hour
18,153
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
2.60
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
377,678.44
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
815,785
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
2.60
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
3.91
to
1
Calculated
Cloth
Area:
208,455
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
2.16
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
377,678
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
2,547,198
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,260,155
(
4K<
area<
16K)
Insulation
Add­
on
$
171,830
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
2,857,212
(
4K<
area<
60K)
Stainless
steel
add­
on
$
1,799,298
(
20K<
area
<
60K
Insulation
add­
on
$
126,522
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
2,106,559
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,725,527
(
4K<
area<
16K)
Insulation
add­
on
$
353,047
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
3,369,213
(
4K<
area<
24K)
Stainless
steel
add­
on
$
1,605,891
(
4K<
area<
24K)
Insulation
add­
on
$
1,035,777
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
1,773,737
(
10K<
area<
115
Stainless
steel
add­
on
$
782,332
(
10K<
area<
115
Insulation
add­
on
$
348,728
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
2,683,843
(
75K<
area<
550
Stainless
steel
add­
on
$
821,125
(
75K<
area<
550
Insulation
add­
on
$
295,530
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
2,979,373
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.01
$/
square
foot
Calculated
Bag
Cost:
$
381,455
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
1,826,749
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
5,187,577
Instrumentation
$
518,758
Sales
Taxes
$
155,627
Freight
$
259,379
Purchased
Equipment
Cost,
PEC
$
6,121,341
Direct
Installation
Costs
Foundations
and
supports
$
244,854
Handling
and
erection
$
3,060,671
Electrical
$
489,707
Piping
$
61,213
Insulation
for
ductwork
$
428,494
Painting
$
122,427
Direct
Installation
Costs
$
4,407,366
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
10,528,707
Indirect
Costs
(
installation)
Engineering
$
612,134
Construction
and
Field
Expense
$
1,224,268
Contractor
Fees
$
612,134
Start­
up
$
61,213
Performance
Test
$
61,213
Contingencies
$
183,640
Total
Indirect
Costs,
IC
$
2,754,603
TOTAL
CAPITAL
INVESTMENT,
TCI
$
35,433,392
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
35,433,392
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
143,023
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
6,597
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
67,583
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
251,507
Shaker
$
251,507
Pulse­
jet
$
368,134
Enter
appropriate
DC
$
368,134
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
708,668
Property
taxes
TCI
*
0.01
$
354,334
Insurance
TCI
*
0.01
$
354,334
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
3,298,933
Total
Indirect
Costs,
IC
$
4,736,851
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
5,473,119
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
subbbituminous
half
volume
for
2
baghouses
half
volume
for
2
baghouses
half
volume
for
2
baghouses
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
half
volume
for
2
baghouses
half
volume
for
2
baghouses
half
volume
for
2
baghouses
$
21.72
$/
acfm
$
70.87
$/
kW
Cost
doubled
for
2
baghouses,
less
5
%
109,946
kWh
$
116,627
278
tons
solid
waste
Set
for
auto
$
6.71
$/
acfm
$
10.95
$/
kW
Direct
cost
doubled
for
2
baghouses
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
100
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
326,314
acfm
Collection
rate,
pounds
per
hour
7,261
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
2.60
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
151,071.38
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
326,314
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
2.60
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
3.91
to
1
Calculated
Cloth
Area:
83,382
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
3.91
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
83,382
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
565,111
(
4K<
area<
16K)
Stainless
steel
add­
on
$
287,210
(
4K<
area<
16K)
Insulation
Add­
on
$
39,397
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
659,994
(
4K<
area<
60K)
Stainless
steel
add­
on
$
416,398
(
20K<
area
<
60K
Insulation
add­
on
$
27,933
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
472,624
(
4K<
area<
16K)
Stainless
steel
add­
on
$
389,126
(
4K<
area<
16K)
Insulation
add­
on
$
79,057
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
754,388
(
4K<
area<
24K)
Stainless
steel
add­
on
$
354,541
(
4K<
area<
24K)
Insulation
add­
on
$
228,521
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
413,204
(
10K<
area<
115
Stainless
steel
add­
on
$
193,150
(
10K<
area<
115
Insulation
add­
on
$
87,128
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
934,838
(
75K<
area<
550
Stainless
steel
add­
on
$
269,024
(
75K<
area<
550
Insulation
add­
on
$
113,978
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
982,909
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.60
$/
square
foot
Calculated
Bag
Cost:
$
134,995
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
520,164
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
1,638,068
Instrumentation
$
163,807
Sales
Taxes
$
49,142
Freight
$
81,903
Purchased
Equipment
Cost,
PEC
$
1,932,920
Direct
Installation
Costs
Foundations
and
supports
$
77,317
Handling
and
erection
$
966,460
Electrical
$
154,634
Piping
$
19,329
Insulation
for
ductwork
$
135,304
Painting
$
38,658
Direct
Installation
Costs
$
1,391,702
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
3,324,622
Indirect
Costs
(
installation)
Engineering
$
193,292
Construction
and
Field
Expense
$
386,584
Contractor
Fees
$
193,292
Start­
up
$
19,329
Performance
Test
$
19,329
Contingencies
$
57,988
Total
Indirect
Costs,
IC
$
869,814
TOTAL
CAPITAL
INVESTMENT,
TCI
$
5,888,794
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
5,888,794
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
50,615
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
2,639
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
27,033
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
114,591
Shaker
$
114,591
Pulse­
jet
$
115,524
Enter
appropriate
DC
$
115,524
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
117,776
Property
taxes
TCI
*
0.01
$
58,888
Insurance
TCI
*
0.01
$
58,888
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
539,677
Total
Indirect
Costs,
IC
$
795,812
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
911,336
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
subbbituminous
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
$
18.05
$/
acfm
$
58.89
$/
kW
56,418
kWh
$
933
111
tons
solid
waste
Set
for
auto
$
2.79
$/
acfm
9.11
$/
MW
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
975
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
760,467
acfm
Collection
rate,
pounds
per
hour
11,542
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
1.77
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
352,067.85
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
760,467
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
1.77
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
4.00
to
1
Calculated
Cloth
Area:
189,893
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
2.16
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
352,068
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
2,374,711
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,175,486
(
4K<
area<
16K)
Insulation
Add­
on
$
160,306
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
2,666,004
(
4K<
area<
60K)
Stainless
steel
add­
on
$
1,678,954
(
20K<
area
<
60K
Insulation
add­
on
$
117,943
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
1,964,369
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,609,229
(
4K<
area<
16K)
Insulation
add­
on
$
329,203
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
3,141,663
(
4K<
area<
24K)
Stainless
steel
add­
on
$
1,496,994
(
4K<
area<
24K)
Insulation
add­
on
$
965,527
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
1,655,340
(
10K<
area<
115
Stainless
steel
add­
on
$
731,060
(
10K<
area<
115
Insulation
add­
on
$
325,963
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
2,531,639
(
75K<
area<
550
Stainless
steel
add­
on
$
773,079
(
75K<
area<
550
Insulation
add­
on
$
279,731
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
2,811,370
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.01
$/
square
foot
Calculated
Bag
Cost:
$
355,589
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
2,362,798
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
5,529,756
Instrumentation
$
552,976
Sales
Taxes
$
165,893
Freight
$
276,488
Purchased
Equipment
Cost,
PEC
$
6,525,113
Direct
Installation
Costs
Foundations
and
supports
$
261,005
Handling
and
erection
$
3,262,556
Electrical
$
522,009
Piping
$
65,251
Insulation
for
ductwork
$
456,758
Painting
$
130,502
Direct
Installation
Costs
$
4,698,081
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
11,223,194
Indirect
Costs
(
installation)
Engineering
$
652,511
Construction
and
Field
Expense
$
1,305,023
Contractor
Fees
$
652,511
Start­
up
$
65,251
Performance
Test
$
65,251
Contingencies
$
195,753
Total
Indirect
Costs,
IC
$
2,936,301
TOTAL
CAPITAL
INVESTMENT,
TCI
$
73,950,905
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
73,950,905
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
133,324
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
6,149
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
42,970
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
216,748
Shaker
$
319,238
Pulse­
jet
$
325,466
Enter
appropriate
DC
$
325,466
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
1,479,018
Property
taxes
TCI
*
0.01
$
739,509
Insurance
TCI
*
0.01
$
739,509
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
6,937,815
Total
Indirect
Costs,
IC
$
9,916,433
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
11,218,299
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
bituminous
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
quarter
volume
for
4
baghouses
$
24.31
$/
acfm
$
75.85
$/
kW
Cost
quadrupled
for
4
baghouses,
less
7
%
102,490
kWh
$
108,719
177
tons
solid
waste
Set
for
auto
$
14.75
$/
acfm
$
11.51
$/
kW
Direct
cost
quadrupled
for
4
baghouses
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
500
MW,

5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
779,966
acfm
Collection
rate,
pounds
per
hour
11,838
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
1.77
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
361,095.23
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
779,966
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
1.77
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
4.00
to
1
Calculated
Cloth
Area:
194,763
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
2.16
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
361,095
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.
Intermittent
Shaker
Filters
Cost
without
bags
$
2,435,510
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,205,331
(
4K<
area<
16K)
Insulation
Add­
on
$
164,368
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
2,733,402
(
4K<
area<
60K)
Stainless
steel
add­
on
$
1,721,373
(
20K<
area
<
60K
Insulation
add­
on
$
120,967
(
20K<
area
<
60K
Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
2,014,489
(
4K<
area<
16K)
Stainless
steel
add­
on
$
1,650,222
(
4K<
area<
16K)
Insulation
add­
on
$
337,608
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
3,221,871
(
4K<
area<
24K)
Stainless
steel
add­
on
$
1,535,379
(
4K<
area<
24K)
Insulation
add­
on
$
990,289
(
4K<
area<
24K)

Reverse­
Air
Filters
Cost
without
bags
$
1,697,073
(
10K<
area<
115
Stainless
steel
add­
on
$
749,133
(
10K<
area<
115
Insulation
add­
on
$
333,988
(
10K<
area<
115
Custom­
built
Filters
Cost
without
bags
$
2,585,289
(
75K<
area<
550
Stainless
steel
add­
on
$
790,015
(
75K<
area<
550
Insulation
add­
on
$
285,300
(
75K<
area<
550
Enter
the
estimated
bare
baghouse
cost
from
above
$
2,870,589
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.
Enter
the
Bag
Price
Factor
1.01
$/
square
foot
Calculated
Bag
Cost:
$
364,706
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
1,783,235
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
5,018,530
Instrumentation
$
501,853
Sales
Taxes
$
150,556
Freight
$
250,927
Purchased
Equipment
Cost,
PEC
$
5,921,866
Direct
Installation
Costs
Foundations
and
supports
$
236,875
Handling
and
erection
$
2,960,933
Electrical
$
473,749
Piping
$
59,219
Insulation
for
ductwork
$
414,531
Painting
$
118,437
Direct
Installation
Costs
$
4,263,743
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
10,185,609
Indirect
Costs
(
installation)
Engineering
$
592,187
Construction
and
Field
Expense
$
1,184,373
Contractor
Fees
$
592,187
Start­
up
$
59,219
Performance
Test
$
59,219
Contingencies
$
177,656
Total
Indirect
Costs,
IC
$
2,664,840
TOTAL
CAPITAL
INVESTMENT,
TCI
$
34,278,728
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
34,278,728
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
136,743
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
6,307
Cost
per
kiloWatt
hour
0.060
$/
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
Waste
Disposal
$
44,072
Cost
per
ton
of
waste
$
50
$/
ton
Total
Direct
Cost,
DC
Reverse­
air
$
221,426
Shaker
$
326,544
Pulse­
jet
$
332,932
Enter
appropriate
DC
$
332,932
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
685,575
Property
taxes
TCI
*
0.01
$
342,787
Insurance
TCI
*
0.01
$
342,787
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
3,191,949
Total
Indirect
Costs,
IC
$
4,583,680
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
5,249,544
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
bituminous
half
volume
for
2
baghouses
half
volume
for
2
baghouses
half
volume
for
2
baghouses
K)
K)
K)

K)
0K)
0K)

K)
K)
K)

'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
'
98
eqn
half
volume
for
2
baghouses
half
volume
for
2
baghouses
half
volume
for
2
baghouses
$
21.97
$/
acfm
$
68.56
$/
kW
Cost
doubled
for
2
baghouses,
less
5
%
105,118
kWh
$
111,506
181
tons
solid
waste
Set
for
auto
$
6.73
$/
acfm
$
10.50
$/
kW
Direct
cost
doubled
for
2
baghouses
CONTROL
COST
METHODS
FOR
BAGHOUSES
Section
5.2
­
Design
Procedures
This
case
is
for
a
unit
of
100
MW,
bituminous
5.2.1
­
Gas
to
Cloth
Ratio
You
enter
items
in
italics
Shaker/
Reverse
Air
Flue
Rate,
cubic
feet
per
minute
311,986
acfm
Collection
rate,
pounds
per
hour
4,735
lb/
hr
Table
5.3
Section
A
Factor
2.00
to
1
ratio
Table
5.3
Section
B
Factor
0.90
Calculated
Grain
Loading:
1.77
gr/
cf
Table
5.3
Section
C
Factor
1.20
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min:
2.16
to
1
Calculated
Cloth
Area:
144,437.96
square
feet
Pulse
Jet
Inlet
Temperature,
degrees
Fahrenheit
320
degrees
F
Flue
Rate,
cubic
feet
per
minute
311,986
cfm
Mean
Particle
Diameter,
micrometers
4
micrometers
Inlet
Dust
Loading,
grains/
cubic
foot
1.77
gr/
cf
Material
Factor
(
see
OAQPS
p.
5­
21)
8.00
Application
Factor
(
see
OAQPS
p.
5­
21)
0.80
Calculated
Gas­
to­
Cloth
Ratio,
ft/
min
4.00
to
1
Calculated
Cloth
Area:
77,905
square
feet
Enter
Desired
Gas­
to­
Cloth
Ratio:
4.00
to
1
Section
5.2.2
­
Pressure
Drop
See
Section
5.2.2,
page
5­
23,
of
the
OAQPS
Control
Cost
Manual.

Enter
Desired
Pressure
Drop:
5
in.
WC
Section
5.3
­
Estimating
Total
Capital
Investment
Section
5.3.1.1
­
Bare
Baghouse
Costs
Gross
Cloth
Area
is
77,905
square
feet
for
type
you
choose.
If
this
value
is
less
than
4,000
square
feet,
then
further
calculations
are
not
valid.
Some
cases
may
have
higher
restrictions;
check
the
notes
below.

Intermittent
Shaker
Filters
Cost
without
bags
$
528,223
(
4K<
area<
16K)
Stainless
steel
add­
on
$
269,104
(
4K<
area<
16K)
Insulation
Add­
on
$
36,932
(
4K<
area<
16K)

Continuous
Shaker
Filters
Cost
without
bags
$
619,103
(
4K<
area<
60K)
Stainless
steel
add­
on
$
390,662
(
20K<
area
<
60K)
Insulation
add­
on
$
26,098
(
20K<
area
<
60K)

Pulse­
jet
Filters
(
Common
Housing)

Cost
without
bags
$
442,216
(
4K<
area<
16K)
Stainless
steel
add­
on
$
364,255
(
4K<
area<
16K)

C­
90
Insulation
add­
on
$
73,957
(
4K<
area<
16K)

Pulse­
jet
Filters
(
Modulars)

Cost
without
bags
$
705,725
(
4K<
area<
24K)
'
98
eqn
Stainless
steel
add­
on
$
331,253
(
4K<
area<
24K)
'
98
eqn
Insulation
add­
on
$
213,498
(
4K<
area<
24K)
'
98
eqn
Reverse­
Air
Filters
Cost
without
bags
$
387,884
(
10K<
area<
115
'
98
eqn
Stainless
steel
add­
on
$
182,186
(
10K<
area<
115
'
98
eqn
Insulation
add­
on
$
82,260
(
10K<
area<
115
'
98
eqn
Custom­
built
Filters
Cost
without
bags
$
902,289
(
75K<
area<
550
'
98
eqn
Stainless
steel
add­
on
$
258,750
(
75K<
area<
550
'
98
eqn
Insulation
add­
on
$
110,600
(
75K<
area<
550
'
98
eqn
Enter
the
estimated
bare
baghouse
cost
from
above
$
919,223
Set
for
auto
Section
5.3.1.2
­
Bag
Costs
Refer
to
Table
5.7
on
page
5­
37
of
the
OAQPS
CCM.

Enter
the
Bag
Price
Factor
1.60
$/
square
foot
Calculated
Bag
Cost:
$
126,172
Section
5.3.1.3
­
Auxiliary
Equipment
Refer
to
page
5­
38
of
the
OAQPS
CCM.
Auxiliary
costs
can
include
Ductwork,
Fan,
Motor,
Starter,
Dampers,
Compressor,
Screw
Conveyor,
and
Stack.
Example
aux.
costs
are
$
62,700.

Enter
any
auxiliary
cost:
$
494,689
Set
for
auto
Table
5­
8.
Capital
Cost
Factors
for
Fabric
Filters
Direct
Costs
Purchased
Equipment
Costs
Fabric
Filter
+
Bags
+
Aux.
Equipment
$
1,540,084
Instrumentation
$
154,008
Sales
Taxes
$
46,203
Freight
$
77,004
Purchased
Equipment
Cost,
PEC
$
1,817,299
Direct
Installation
Costs
Foundations
and
supports
$
72,692
Handling
and
erection
$
908,649
Electrical
$
145,384
Piping
$
18,173
Insulation
for
ductwork
$
127,211
Painting
$
36,346
Direct
Installation
Costs
$
1,308,455
Site
Preparation
as
required,
Buildings
as
required,

Total
Direct
Cost
$
3,125,754
Indirect
Costs
(
installation)
Engineering
$
181,730
C­
91
Construction
and
Field
Expense
$
363,460
Contractor
Fees
$
181,730
Start­
up
$
18,173
Performance
Test
$
18,173
Contingencies
$
54,519
Total
Indirect
Costs,
IC
$
817,784
TOTAL
CAPITAL
INVESTMENT,
TCI
$
5,536,545
$
17.75
$/
acfm
$
55.37
$/
kW
Section
5.4
­
Estimating
Total
Annual
Cost
Table
5.10
page
5­
49,
OAQPS
Control
Cost
Manual
(
EPA
450/
3­
90­
006,
January
1990)
Annual
Costs
for
Fabric
Filters
Total
Capital
Investment
(
from
previous
table)
$
5,536,545
Cost
Item
Factor
Cost
Direct
Annual
Costs,
DC
Operating
Labor
Operator
$
10,701
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.26
$/
hr
Supervisor
15%
of
operator
$
1,605
Operating
materials
­
$
0
Maintenance
Labor
$
10,999
Hours/
day
2
hr/
d
Days/
year
310
d/
yr
Dollars/
hour
17.74
$/
hr
Material
Equal
to
Maint.
Labor
$
10,999
Replacement
Parts
(
bags)
$
47,307
Labor
replacement
rate
0.19
$/
sq.
ft.

Utilities
Electricity,
$/
kWh
$
2,523
Cost
per
kiloWatt
hour
0.060
$/
kWh
53,941
kWh
Hours
per
year
operation
7,446
hr/
yr
Compressed
Air
(
dried
and
filtered)
­
Pulse
Jet
Only
$
892
Waste
Disposal
$
17,628
Cost
per
ton
of
waste
$
50
$/
ton
73
tons
solid
waste
Total
Direct
Cost,
DC
Reverse­
air
$
101,762
Shaker
$
101,762
Pulse­
jet
$
102,654
Enter
appropriate
DC
$
102,654
Set
for
auto
Indirect
Annual
Costs,
IC
Overhead
Sixty
percent
of
sum
of
$
20,582
operating,
supv.,
&
maint.
labor
&
maint.
materials
Administrative
charges
TCI
*
0.02
$
110,731
Property
taxes
TCI
*
0.01
$
55,365
Insurance
TCI
*
0.01
$
55,365
C­
92
Capital
recovery
CRF
*
TCI
CRF
=
0.09439293
$
507,485
Total
Indirect
Costs,
IC
$
749,530
Total
Annual
Cost,
TAC
TAC
=
DC
+
IC
$
852,184
$
2.73
$/
acfm
8.52
$/
MW
*
based
on
user­
provided
hours/
year
of
operation
CRF:
The
capital
recovery
factor,
CRF,
is
a
function
of
the
equipment
life
(
typically
10
years)
and
the
opportunity
cost
of
the
capital
(
i.
e.,
interest
rate).
For
example,
for
a
20
year
equipment
life
and
a
10%
interest
rate,
CRF
=
0.1175.

CRF
=
0.094393
bag
life
4
years
interest
0.07
fraction
eqpt
life
20
years
C­
93
Spray­
drier
adsorber
for
100
MW
bituminous
acfm
pump
as
%
of
spray
dr
Gas
flow,
acfm
3,000
311,986
1000
0.054
1000
Temperature
in,
oF
320
3000
0.095
3000
Temperature
out,
oF
260
5,000
0.124
5,000
Retrofit
factor
1.2
10,000
0.179
10,000
TCI
spray
drier
681,789
15,000
0.222
15,000
Water,
lb/
h
240
20,000
0.259
20,000
TCI
pump
64,504
30,000
0.322
50,000
TCI
spray
drier
system
746,293
50,000
0.424
300,000
1.115
0.094609936
1,000,000
2.135
Equipment
life,
yrs
15
MW
$/
kW
operating
time,
h/
y
8400
150
133000
Heat
of
vapor.
H2O,
Btu/
lb
970
267
231000
Heat
cap,
H2O
vapor,
Btu/
lb­
oF
0.44
300
166000
Heat
cap,
air,
Btu/
lb­
oF
0.25
362
172000
Heat
cap,
water,
Btu/
lb­
oF
0.0022
500
152232.8
Vaporization,
temp,
oF
212
500
160090
Temp.
of
H2O
entering,
oF
77
508
189000
Lime
cost,
$/
ton
53
Water
cost,
$/
gal
0.0002
labor
cost,
$/
h
17.26
maintenance
labor,
$/
h
17.74
bit
sub
lignite
TCI
spray
drier
TCI
spray
drier
system$/
acfm
$/
MW
411,315
1000
433,684
1000
434
1,304,955
681,789
3000
746,293
3000
249
748,532
862,384
5,000
969,023
5,000
194
583,158
1,186,245
10,000
1,398,222
10,000
140
420,725
1,429,475
15,000
1,746,789
15,000
116
350,406
1,631,730
20,000
2054382
20,000
103
309,082
2,487,142
50,000
3,452,604
50,000
69
207,778
MW
$/
y­
kW
150
267
300
362
500
41.50
500
44.30
508
Capital
cost,
$
Annual
cost,
$/
MW­
y
Power,
kWh/
y­
MW
Water,
gal/
y­
MW
solid
waste,
9.8504x
+
168263­
28000
44360
81,883
289,000
202
9.8504x
+
168263
41500
89,321
359,834
111
9.8504x
+
168263+
45000
48000
93,500
414,375
149
SDA
cost,
$/
MW
y
=
­
0.062x
+
185.62
R2
=
0.048
0
50
100
150
200
250
0
200
400
600
Unit
size,
MW
Capital
cost,

$/
MW
SDA
cost,
$/
MW
y
=
9.8504x
+
168263
R2
=
0.0019
0
100000
200000
300000
0
200
400
600
Unit
size,
MW
SDA
cost,
1999
$/
MW
te,
ton/
y­
MW
­
above
fly
ash
COMBUSTION
CALCULATIONS
Bituminous
Ultimate
Mass
of
O2
Required
Mass
of
Products
Analysis­%
per
lb
of
Fuel
per
lb
of
Fuel
Carbon
72.3
1.93
2.65
Hydrogen
5.5
0.44
0.56
Sulfur
1.8
0.018
0.036
Nitrogen
1.4
0.014
Oxygen
12.6
Moisture
6.5
Excess
Air­%
20
Combustion
Air
Moisture­
0.0054
(
Default
value,
50%
relative
humidity
at
60
F
=
lbs
H2O/
lb
dry
air
0.0054;
range
=
0.0011
@
10%
to
0.011
@
100%)

O2
Req'd
w/
o
Excess
Air
2.26
lbs
Additional
O2
w/
Excess
Air
0.45
lbs
Total
O2
w/
Excess
Air
2.71
lbs
Total
Dry
Air
Req'd
11.69
lbs
(
including
Excess
Air)
Note:
Combustion
Air
Req'd,
dry
144.70
SCFD
per
lb
of
fuel
Standard
conditions
Combustion
Air
Req'd,
wet
145.96
SCFW
per
lb
of
fuel
for
these
calculations
are
32
F
and
29.92
inches
Flue
Gas
Volume,
dry
142.18
SCFD
per
lb
of
fuel
of
mercury.
Flue
Gas
Volume,
wet
154.60
SCFW
per
lb
of
fuel
Flue
Gas
Density
@
Std
0.0824925
lbs
per
SCFW
Conditions
(
32
F,
29.92
in
HG)

Molecular
Weight
of
Flue
29.61
lbs
per
lb­
mole
Gas
FLUE
GAS
ANALYSIS
Dry
Gas
Wet
Gas
Constituent
Mole
%
Mole
%
CO2
15.21
13.99
SO2
0.14
0.13
O2
3.57
3.28
N2
81.08
74.56
H2O
8.04
acfm/
MW
@
320
oF
100
MW
500
MW
975
MW
acfm/
10,000,000
Btu
per
h
@
320
3,119.86
311,986
1,559,931
3,041,866
=
acfm/
MW
76,372
381,862
744,630
MW
x
187.19
=
acfm
@
320
oF
4,735
23,675
46,167
subbituminous
3,263.14
326,314
1,631,571
3,181,563
94,097
476,884
929,923
7,261
36,800
71,759
lignite
3,428.39
342,839
1,714,194
3,342,678
144,352
721,761
1,407,434
9,527
47,636
92,891
Logan
­
bit
3,016
St
Clair
­
0.85
sub/
0.15
bit
2,948
San
Juan
­
lignite
3,507
Monticello
1
­
lignite
3,371
Monticello
3
­
lignite
3,338
oil
­
acfm/
MW
2,999
Carbon
Hydrogen
Sulfur
Nitrogen
Oxygen
Moisture
Btu/
lb
ash
Data
from
P
bit
"
as
receive
84
4.8
0.6
1.1
5.6
3.5
99.6
14550
3.9
1.3
3.1
4.4
14290
5.1
76.6
5.2
1.3
1.6
6.2
2.6
93.5
13610
9.1
79.2
5.7
0.6
1.5
10
3.1
100.1
14290
3
68.4
5.6
1.2
1.4
16.4
8.2
101.2
12160
7
71.5
5.8
2.6
1.6
14.3
7.2
103
12950
4.2
62.8
5.9
4.3
1
17.4
12.1
103.5
11480
8.6
63.4
5.7
2.3
1.3
18.6
12.4
103.7
11420
8.7
72.3
5.5
1.8
1.4
12.6
6.5
100.1
13,094
6.2
average
10255.34
9629.428
F­
factor
sub
54.6
6.4
0.4
1
33.8
16.5
9740
11.2
2.1
23.2
9420
3.8
1.1
24.6
8610
7.8
54.6
6.4
1.2
1
33.8
21.43333
118.4333
10,485
7.7
average
8785.149
F­
factor
lig
35.71
2.29
0.48
0.64
14.18
40.00
5940
6.7
Combustion
42.4
2.8
0.7
0.7
12.4
34.8
7210
6.2
Combustion
42.5
3.1
0.5
0.8
12.1
33.7
7350
7.3
Combustion
42.4
6.7
0.7
1.7
43.3
34.8
7210
6.2
Perry
40.75
3.72
0.59
0.96
20.49
35.83
102.35
6,927.50
6.60
average
9664.292
F­
factor
3340.23
3016.261
acfm
lb/
h
coal
lb/
h
ash
acfm
lb/
h
coal
lb/
h
ash
acfm
lb/
h
coal
lb/
h
ash
Perry,
4th
ed.,
p.
9­
3
ved"

142
dscf/
lb
103
98.61
76.37086
lb
coal/
MM
94.09993
138.6963
10844.66
F­
factor
9692.293
13676.84
3119.863
150.5775
scfm
~
bit
for
same
Btu
1.031655
x
gas
volume
for
same
Btu
tion
p.
11­
9
tion
p.
C­
11
tion
p.
C­
11
163.2364
scfm
~
bit
for
same
Btu
1.118386
x
gas
volume
for
same
Btu
COMBUSTION
CALCULATIONS
Subbituminous
Ultimate
Mass
of
O2
Required
Mass
of
Products
Analysis­%
per
lb
of
Fuel
per
lb
of
Fuel
Carbon
54.6
1.46
2.00
Carbon
Hydrogen
6.4
0.512
0.79
bit
Sulfur
1.2
0.012
0.024
84
Nitrogen
1
0.01
Oxygen
33.8
76.6
Moisture
21.4
79.2
68.4
Excess
Air­%
20
71.5
62.8
Combustion
Air
Moisture­
0.0054
(
Default
value,
50%
relative
humidity
at
60
F
=
63.4
lbs
H2O/
lb
dry
air
0.0054;
range
=
0.0011
@
10%
to
0.011
@
100%)
72.3
sub
O2
Req'd
w/
o
Excess
Air
1.64
lbs
54.6
Additional
O2
w/
Excess
Air
0.33
lbs
Total
O2
w/
Excess
Air
1.97
lbs
Total
Dry
Air
Req'd
8.49
lbs
54.6
(
including
Excess
Air)
Note:
lig
Combustion
Air
Req'd,
dry
105.13
SCFD
per
lb
of
fuel
Standard
conditions
42.4
Combustion
Air
Req'd,
wet
106.04
SCFW
per
lb
of
fuel
for
these
calculations
are
32
F
and
29.92
inches
Flue
Gas
Volume,
dry
103.90
SCFD
per
lb
of
fuel
of
mercury.
Flue
Gas
Volume,
wet
120.57
SCFW
per
lb
of
fuel
Flue
Gas
Density
@
Std
0.080639
lbs
per
SCFW
Conditions
(
32
F,
29.92
in
HG)

Molecular
Weight
of
Flue
28.95
lbs
per
lb­
mole
Gas
FLUE
GAS
ANALYSIS
Dry
Gas
Wet
Gas
Constituent
Mole
%
Mole
%
CO2
15.72
13.55
SO2
0.13
0.11
O2
3.55
3.06
N2
80.60
69.46
H2O
13.83
Hydrogen
Sulfur
Nitrogen
Oxygen
Moisture
Btu/
lb
ash
4.8
0.6
1.1
5.6
3.5
99.6
14550
3.9
1.3
3.1
4.4
14290
5.1
5.2
1.3
1.6
6.2
2.6
93.5
13610
9.1
5.7
0.6
1.5
10
3.1
100.1
14290
3
5.6
1.2
1.4
16.4
8.2
101.2
12160
7
5.8
2.6
1.6
14.3
7.2
103
12950
4.2
5.9
4.3
1
17.4
12.1
103.5
11480
8.6
5.7
2.3
1.3
18.6
12.4
103.7
11420
8.7
5.5
1.8
1.4
12.6
6.5
100.1
13,094
6.2
6.4
0.4
1
33.8
16.5
9740
11.2
2.1
23.2
9420
3.8
1.1
24.6
8610
7.8
6.4
1.2
1
33.8
21.43333
118.4333
10,627
7.7
6.7
0.7
1.7
43.3
34.8
7210
6.2
COMBUSTION
CALCULATIONS
Lignite
Ultimate
Mass
of
O2
Required
Mass
of
Products
Analysis­%
per
lb
of
Fuel
per
lb
of
Fuel
Carbon
40.75
1.09
1.49
Carbon
Hydrogen
3.72
0.2976
0.6931
bit
Sulfur
0.59
0.0059
0.0118
84
Nitrogen
0.96
0.0096
Oxygen
20.49
76.6
Moisture
35.83
79.2
68.4
Excess
Air­%
20
71.5
62.8
Combustion
Air
Moisture­
0.0054
(
Default
value,
50%
relative
humidity
at
60
F
=
63.4
lbs
H2O/
lb
dry
air
0.0054;
range
=
0.0011
@
10%
to
0.011
@
100%)
72.3
sub
O2
Req'd
w/
o
Excess
Air
1.19
lbs
54.6
Additional
O2
w/
Excess
Air
0.24
lbs
Total
O2
w/
Excess
Air
1.42
lbs
Total
Dry
Air
Req'd
6.13
lbs
54.6
(
including
Excess
Air)
Note:
lig
Combustion
Air
Req'd,
dry
75.89
SCFD
per
lb
of
fuel
Standard
conditions
35.71
Combustion
Air
Req'd,
wet
76.55
SCFW
per
lb
of
fuel
for
these
calculations
42.4
are
32
F
and
29.92
inches
42.5
Flue
Gas
Volume,
dry
75.40
SCFD
per
lb
of
fuel
of
mercury.
42.4
Flue
Gas
Volume,
wet
89.89
SCFW
per
lb
of
fuel
40.75
Flue
Gas
Density
@
Std
0.07996
lbs
per
SCFW
Conditions
(
32
F,
29.92
in
HG)

Molecular
Weight
of
Flue
28.70
lbs
per
lb­
mole
Gas
FLUE
GAS
ANALYSIS
Dry
Gas
Wet
Gas
Constituent
Mole
%
Mole
%
CO2
16.17
13.56
SO2
0.09
0.07
O2
3.53
2.96
N2
80.22
67.29
H2O
16.11
Hydrogen
Sulfur
Nitrogen
Oxygen
Moisture
Btu/
lb
ash
4.8
0.6
1.1
5.6
3.5
99.6
14550
3.9
1.3
3.1
4.4
14290
5.1
5.2
1.3
1.6
6.2
2.6
93.5
13610
9.1
5.7
0.6
1.5
10
3.1
100.1
14290
3
5.6
1.2
1.4
16.4
8.2
101.2
12160
7
5.8
2.6
1.6
14.3
7.2
103
12950
4.2
5.9
4.3
1
17.4
12.1
103.5
11480
8.6
5.7
2.3
1.3
18.6
12.4
103.7
11420
8.7
5.5
1.8
1.4
12.6
6.5
100.1
13,094
6.2
6.4
0.4
1
33.8
16.5
9740
11.2
2.1
23.2
9420
3.8
1.1
24.6
8610
7.8
6.4
1.2
1
33.8
21.43333
118.4333
10,627
7.7
2.29
0.48
0.64
14.18
40.00
5940
6.7
Combustion
p.
11­
9
2.8
0.7
0.7
12.4
34.8
7210
6.2
Combustion
p.
C­
11
3.1
0.5
0.8
12.1
33.7
7350
7.3
Combustion
p.
C­
11
6.7
0.7
1.7
43.3
34.8
7210
6.2
Perry
3.72
0.59
0.96
20.49
35.83
102.35
6,927.50
6.60
average
163.2364
9664.292
F­
factor
2.132475
