p. 1



# OAR Box 

# 1828 Prepped byOllie Stewart



# Document

Number: 

# 280 ) ll-K - 

# (I ) -9 3
Docket Number: 

# A-83-2 7

Printed 11/12/200811:12:58AM Sheet 280of 325ft

199 0 PROJECTE DNE M INDUSTRIA

L FOSSI L FUEL-FIRE

DDOILE R AIREMISSIONS , FUEL DEMAND , AN DCOST S
(5T H ROUN DS0 2 NSP S ANALYSI S — HIGHE ROI L AN

O GA S PRICES ) (BAS E CAS E AN

DOPTIO N CASE S 5-7 )

PREPARE DFOR : THE U.S . ENVIRONMENTA L PROTECTIO

N AGENC Y

PREPARE DBY : ENERG YAN DENVIRONMENTA

L ANALYSIS , INC . 165 5 NORT

H FOR T MYE RDRIV E ARLINGTON , VIRGINI A 22Z0 9 07/26/8 4



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1 

### iNOTE S O N IFCA M PROJECTION S «*K*»»*«X#*«H*<*<****»»t*!**)*»IM>l*<*X *

1 . REVISE

DNAT H SCRUBBE

RCOST S LS DrC DRESTRICTL

DT O LO W SULFU RCOA L TYPE S ( B AN

O DONLY) • INCLUDE S ESTIMATE S O F INTERES T DURIN

GCONSTRUCTION . 2 . BAS E CAS E

- S02 : CURREN

T NSP S

- PM : PROPOSE

DNSP S (4 9 F

R25103 )

- NOX : LE

A O RSC A REQUIRE

D( > 10 0 MMBTU/HR ) 3 . OPTIO

N CASE S 1- 4

- PRESENTE

DI N A SEPERAT E REPORT
<• . OPTIO

N CAS E 5

- COA L TYP E B , 0. 8 AN

O 0. 3 PERCEN

T SULFU RRESIDUA

L FUEL OIL S AR E COMPLIANCE FUEL S

- A T LEAS T 7 0 PERCEN

T S0 2 REMOVA

L REQUIRE

DO N NON-COMPLIANCE FUEL S 5 . OPTIO

N CAS E 6

- N O COMPLIANCE COA

L TYPE S

- 0- 3 PERCEN

T SULFU RRESIDUA

L FUEL OI L I S IH COMPLIANCE

- A T LEAS T 7 0 PERCEN

T S0 2 REMOVA

L REQUIRE

DO N NON-COHPLIANCE FUEL S 6 . OPTIO

N CAS E 7

- N O COMPLIANCE COA

L TYPE S

- 0. 3 PERCEN

T SULFU RRESIOUA

L FUEL OI L I S I

N COMPLIANCE

- 9 0 PERCEN

T S0 2 REMOVA

L REQUIRE

DO N NON-COMPLIANCE FUEL S

T l C O•

INDUSTRIA L

NATURA L GAS SO * CEILIN

G(LB/MMBTU ) F M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MNBTU ) DISTILLAT E FUE

L OI L so ; CEILIN G(LB/M::DTU I P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU ) RESIDUA L FUEL OI L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LD/MMBTU ) NO XCEILIN

G(LB/MMBTU ) COA L r-O 2 CEILIN

G(LB/MMBTU ) ?: 1 CEILIN

G(LB/MMBTU )

- PO R<30 XC

U NO XCEILINf

e (LB/MMBTU )

RESIDUA L FUEL OI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 RCMOVA

L REQUIRE

O BOILE

RHE W SOURCE PERFORMANCE STANDARD S ASSUMPTION S

LO W SULFU REXEMPTIO

N FO RCOA L (LD/MMBTU ) COA L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

O LO W SULFU REXEMPTIO

N FO RCOA L (LB/MMBTU )

1 OPTIO N

10-3 0

NON E NON E NON E

NON E NON E NON E

HON E NON E NON E

NON E NON E NON E NON E MANOATOR

Y

NON E NON E NON E NON E

NON E NON E HON E HON E CAS E 5 (AR013 5 )

BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T IMPUT ) 30-5 0

NON E NON E NON E

NON E NON E HON E

HON E HON E HON E

NON E NON E HON E NON E SCRUBBIN

G

NON E HON E HON E HON E

NON E NOH E NON E NON E 50-7 5 7 5

NON E NON E NON E

HON E NON E NON E

NON E NON E NON E

NON E HON E NON E HON E REGULATION S

NON E NON E NON E HON E

NON E HON E NON E NON E -10 0

NOM E HON E HON E

HON E NON E NON E

NOH E NON E NON E

NOH E HON E HON E NOH E

NOHE NON E NON E NON E

NON E NON E NON E NON E 100-15 0

HON E HOM E 0.2 0

HON E NON E 0.2 0

0.5 0 NON E 0.3 1

0.5 0 0.0 5 0.2 0 0.6 0

NON E 70.0 0 NON E 0.0 5

NON E 70.0 0 NOHE 1.2 0 150-20 0

NON E NON E 0.2 0

NON E NON E 0.2 0

0.5 0 NON E 0.3 1

0.5 0 0.0 5 0.2 0 0.6 0

NON E 70.0 0 NON E 0.0 5

NON E 70.0 0 HON E 1.2 0 200-25 0

HON E NON E 0.2 0

NOH E HON E 0.2 0

0.5 0 HON E 0.3 1

0.5 0 0.0 5 0.2 0 0.60

_

NON E 70.0 0 HON E 0.65 .
NON E 70.0 0 NON E 1.2 0

i 

## "" X

• 4

>25 0

- NOHE NON E 0.3 0

NON E 0.1 0 0.3 0

0.5 0 0.1 0 0.3 1

0.5 0 0.0 5 0.0 5 0.7 0

NON E 70.0 0 . ' NOHE 0.8 5

NON E 70.0 0 NON E 1.2 0

J

-IHDUSTRIA L BOILE RHE W SOURCE PERFORMAHCE STANDARD S ASSUMPTIONS

NATURA L GAS S0 2 CEILIN

G(LB/MMBTU ) F M CEILIN G(LB/MM3TU ) NO XCEILIN

G(LB/MMBTU ) DISTILLAT E FUEL OI L S0 2 CEILIN

G(LB/MM3TU ) F M CEILIN G(LB/MM5TU ) NO XCEILIN

G(LB/li;;3TU ) RESIDUA L FUE L OI L SO S CEILIN

G(LB/MMBTU ) F M CEILIN G(LB/MM3TU ) NO XCEILIN

G(LB/MMBTU ) COA L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU )

- FC! ? <30 XC

U NO XCEILIN

G(LB/MMBTU )

- RESIDUA L FUE L OI L S0 2 FLOO

R(LB/MMBTU ) PEPCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO W SULFU REXEMPTIO

N FO RCOA L (LB/MMBTU ) COA L S0 2 FLOO

R(LB/MMBTU ) PEPCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO W SULFU REXEMPTIO

N FO RCOA L (LB/MMBTU )

1 OPTIO N

10-3 0

NON E NON E NON E

NON E NON E NON E

HON E HOM E NON E

HON E NON E NOHE NON E MANDATOR

Y

HON E HON E NON E NON E

NON E NON E NON E NON E CAS E 6 (AR013 5 )

BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT ) 30-5 0

NON E HON E NON E

HON E NON E NON E

NOH E NON E NON E

NOHE HON E NON E NON E SCRUBBIN

G

NON E HON E NON E HON E

NON E NOH E NON E NON E 50-7 5 7 5

NOHE NON E HON E

NOHE HON E HON E

HON E NON E HON E

NOHE NON E NOHE NON E REGULATION S

HON E HOHE NON E NON E

NON E NON E HOHE HOHE -10 0

NON E NON E NOHE

HON E NON E HON E

NON E NON E NON E

NON E NON E HON E HON E

NON E NON E NON E NON E

NON E NON E NON E HON E 100-15 0

HON E HON E 0.2 0

NON E NON E 0.2 0

0.5 0 NON E 0.3 1

0.5 0 0.0 5 0.2 0 0.6 0

NON E 70.0 0 NON E 0.3 5

NON E 70.0 0 NON E HOHE 150-20 0

HON E NON E 0.2 0

NON E NON E 0.2 0

0.5 0 NON E 0.3 1

0.5 0 0.0 5 0.2 0 0.6 0

NON E 70.0 0 NON E 0.3 5

NON E 70.0 0 NON E NON E 200-25 0

NON E NON E 0.2 0

NON E NOH E 0.2 0

0.5 0 NON E 0.3 1

0.5 0 0.0 5 0.2 0 0.6 0

NON E 70.0 0 NON E 0.3 5

NON E 70.0 0 NOH E HON E

i >25 0

NOHE HOHE 0.3 0

HOHE 0.1 0 0.3 0

0.5 0 0.1 0 0.3 1

0.5 0 0.0 5 0.0 5 0.7 0

NON E 70.0 0 NON E 0.3 5

HON E 70.0 0 NON E NON EIHDUSTRIA L BOILE RHE M SOURCE PERFORMAHCE STAHDARD S ASSUMPTIOMS OPTIO N CAS E 7 (AR013 5 )

BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )

NATURA L GAS S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MM3TU ) NO XCEILIN

G(LB/MMBTU )
DISTILLAT E FUE

L OILS0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU )
RESIDUA L FUE L OI L S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN

G(LB/MMBTU ) COA L T-0 2 CEILIN

G(LB/MMBTU ) YM CEILIN G(LB/MMBTU )



### - ror? <ZOY. 

### c u NO XCEILIN

G(LB/MMBTU ) 10-3 0

NOHE NON E NON E

NON E HON E HOHE

NOHE HOH E NON E

NON E NON E NON E NON E 30-5 0

NOH E HON E HON E

NOHE HOHE HOH E

NOH E HOH E HON E

NON E NON E NON E NON E 50-7 5

NON E NON E NON E

HON E HON E NON E

NON E NON E NOHE

HON E NON E HON E NON E 75-10 0

NON E NON E NOH E

HOH E HON E HOM E

NON E NON E NOHE

NON E NOH E NON E NOHE 100-15 0

NON E NON E 0.2 0

NON E NOHE 0.2 0

0.6 0 HOH E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 150-20 0

HON E NON E 0.2 0

NON E NON E 0.2 0

0.6 0 NON E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 200-25 0

NON E NOHE 0.2 0

NOHE NON E 0.2 0

0.6 0 NON E 0.3 1

0.6 0 0.0 5 0.2 0 0.6 0 >25 0

NON E NON E 0.3 0

NON E 0.1 0 0.3 0

0.6 0 0.1 0 0.3 1

0.6 0 0.0 5 0.0 5 0.7 0 MANDATOR

YSCRUBBIN

GREGULATION S RESIDUA L FUE L OI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO W SULFU REXEMPTIO

N FO RCOA L (LB/MMBTU )
COA L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO W SULFU REXEMPTIO

N FO RCOA L (LB/MM3TU ) HOHE

HOH E NON E HON E

HOHE NON E NOH E HOH E NON

E NOH E HOHE NON E

NON E NOHE HOHE HON E NOHE HOHE HON E NOHE

NON E NON E HON E NOHE NON

E NOH E HON E NOH E

NON E NON E NON E NOHE NON

E 90.0 0 NON E 0.3 5

NON E 90.0 0 NON E HOHE NON

E 90.0 0 NON E 0.3 5

NON E 90.0 0 NON E HOHE NON

E 90.0 0 NOHE 0.3 5

NON E 90.0 0 NON E NOH E NON

E 90.0 0 HOHE 0.3 5

NON E 90.0 0 NOHE HON ELIS T O F TABLE S

DESCRIPTIO

N O F TABLE TABLE NUMBE R

FUE L DEMAN D

- NUMBE RO F UNIT S 1

- BTU S O

F FUEL CONSUMPTIO

N 2 POLLUTAN

T EMISSION S 3 COST S 4 HO XONL Y

- CONTROL COST S 5

- EMISSION S 6 NATIONA L IMPACT S B

YSIZ E (MMBTU/HR )

- 10-5 0 7

- 50-7 5 8

- 75-10 0 9

- 100-15 0 1 0

- 150-20 0 1 1

- 200-25 0 1 2

- > 25 0 1 3

- > 10 0 1 4

- 100-25 0 1 5

- > 5 0 1 6

- TOTA L 1 7

T lTABL E 1 —199 0 FUE L DEMAHD (HUMBE R OF UNITS )

10-5 0 BOILE R SIZ E (MMBTU/HR )

50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L *TOTAL * THE BAS E OPTIO N OPTION OPTION NATURAL GA S TH E BAS E OPTION OPTIO N OPTION COA L THE BAS E OPTION OPTION OPTION CAS E CAS E 5 CAS E 6 CAS E 7
AN D OI L CAS E CAS E 5 CAS E 6 CAS E 7

CAS E CAS E 5 CAS E 6 CAS E 7 141 2

141 2 141 2 141 2

125 1 125 1 125 1 125 1

16 1 16 1 16 1 16 1 577
.

577
. 577
. 577
.
398
. 393
. 398
. 398
.
179
. 179
. 179
. 179
. 271
.

271
. 271
. 271
.
212
. 239
. 254
. 254
.
59
. 32
. 17
. 17
. 135
.

135
. 135
. 135
.
55
. 71
. 115
. 120
.
80
. 64
. 20
. 15
. 62
.

62
. 62
. 62
.
21
. 26
. 49
. 49
.
41
. 36
. 13
. 13
. 136
.

136
. 136
. 136
.
70
. 70
. 86
. 86
.
66
. 66
. 50
. 50
. 259 3

259 3 259 3 259 3

200 7 205 5 215 3 215 8

58 6 53 8 44 0 43 5

T l 0 0TABL E 2 —199 0 FUE L DEMAH D (10**1 2 BTUS )

10-5 0 BOILE R SIZ E (MMBTU/HR )

50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L *TOTAL * TH E BAS E CAS E OPTIONCAS E 5 OPTIONCAS E 6 OPTIONCAS E 7 NATURAL GA S TH E BAS E CAS E OPTIONCAS E 5 OPTIONCAS E 6 OPTIONCAS E 7 RESIDUAL FUE L OI L THE BAS E CAS E OPTIONCAS E 5 OPTIONCAS E 6 OPTIONCAS E 7 COAL TH E BAS E CAS E OPTIONCAS E 5 OPTIONCAS E 6 OPTIONCAS E 7 132
. 132
. 132
. 132
.
86
. 86
. 86
. 86
.
9
. 9
. 9
. 9
.
36
. 36
. 36
. 36
. 136
.

136
. 136
. 136
.
59
. 59
. 59
. 59
.
6
. 6
. 6
. 6
.
72
. 72
. 72
. 72
. 129
.

129
. 129
. 129
.
82
. 105
. 117
. 117 .
7
. 0
. 0
. 0
.
40
. 23
. 1 * *
. 12
. 111
.

111
. 111
. 111 .
41
. 56
. 68
. 94
.
0
. 0
. 0
. 0
.
70
. 55
. 21
. 17
. 67
.

67
. 67
. 67
.
19
. 24
. 50
. 50
.
0
. 0
. 0
. 0
.
48
. 43
. 17
. 17
. 191
.

191
. 191
. 191 .
65
. 65
. 90
. 90
.
0
. 0
. 0
. 0
.
126
. 126
. 101
. 101
. 766
.

766
. 766 . 766 .
352
. 396
. 490 . 496 .
22
. 15
. 15
. 15
.
392 . 356
. 261
. 255
.

T l C OTABLE 3 — 199 0 EMISSIONS (10** 3 TONS )

10-5 0 BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L S0 2 TH E BAS E OPTIO N OPTIO N OPTIO N P M TH E BAS E OPTIO N OPTIO N OPTIO N NO X TH E BAS E OPTIO N OPTIO N OPTIO N PMI O TH E BAS E OPTIO N OPTIO N OPTIO N CAS E CAS E CAS E CAS E

CAS E CAS E CAS E CAS E

CAS E CAS E CAS E CAS E

CAS E CAS E CAS E CAS E 5 6 7

5 6 7

5 6 7

5 6 7 68 .

68 . 68 . 68 .
11 . 11 . 11 . 11 .
13 . 13 . 13 . 13 .
8 . 8 . 8 . 8 . 121 .

121 . 121 . 121 .
19 . 19 . 19 . 19 .
23 . 23 . 23 . 23 .
14 . 14 . 14 . 14 . 74 .

11 . 2 . 2 .
2 . 1 . 1 . 1 .
17 . 14 . 12 . 12 .
2 . 1 . 1 . 1 . 106 .

26 . 4 . 2 .
1 . 1 . 1 . 1 .
23 . 20 . 15 . 14 .
1 . 1 . 1 . 1 . 86 .

20 . 3 . 2 .
1 . 1 . 1 . 1 .
15 . 14 . 9 . 9 .
1 . 1 . 1 . 1 . 59 .

57 . 17 . 10 .
2 . 2 . 2 .

43 . 43 . 37 . 37 .
2 . 2 . 2 . 2 . 515 .

303 . 216 . 205 .
36 . 35 . 34 . 34 .
134 . 127 . 109 . 108 .
28 . 27 . 26 . 26 .

T l oTABL E 4 —199 0 COST S (10**6 , $1982 )

10-5 0 BOILE R SIZ E (MMBTU/HR )

50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L AHNUALIZE D COST S - TOTAL TH E BAS E CAS E 1322. 7 OPTIONCAS E 5 1322. 7 OPTIONCAS E 6 1322. 7 OPTIONCAS E 7 1322. 7 CAPITA L COST S - TOTA

L THE BAS E CAS E 1584. 9 OPTIONCAS E 5 1584. 9 OPTIONCAS E 6 1584. 9 OPTIONCAS E 7 1584. 9 1159. 6 1159. 6 1159. 6 1159. 6
1881. 4 1831. 4 1091. 4 1881. 4 1008. 0

1008. 7 1011. 1 1011. 2
1294. 3 1021. 1 884. 5 884. 3 837. 6

843. 1 832. 9 829. 4
1521. 2 1296. 5 777. 9 696. 9 493. 1

504. 4 501. 1 501. 1
919. 9 838. 8 495. 4 495. 4 1386. 3

1386. 7 1414. 6 1415. 0
2189. 4 2188. 5 1922. 3 1909. 2 6207. 3

6225. 2 6241. 9 6239. 0
9391. 2 8811. 3 7546. 4 7452. 1TABL E 5 —199 0 NO XCONTRO L ANNUALIZE D COST S (10**6 , $1932 )

10-5 0 BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L •TOTAL * TH E BAS E CAS E OPTIONCAS E 5 OPTIONCAS E 6 OPTIO NCAS E 7 NATURA L GA S AN

DOI L TH E BAS E CAS E OPTIO N CAS E 5 OPTIO N CAS E 6 OPTIO N CAS E 7 COA L TH E BAS E CAS E OPTIO N CAS E 5 OPTIO N CAS E 6 OPTIO N CAS E 7 -4. 1

-4. 1 -4. 1 -4. 1

-4. 0 -4. 0 -4. 0 -4. 0

-0. 1 -0. 1 -0. 1 -0. 1 -4. 9

-4. 9 -4. 9 -4. 9

-4. 2 -4. 2 -4. 2 -4. 2

-0. 6 -0. 6 -0. 6 -0. 6 1. 3

-2. 5 -3. 6 -3. 6

-1. 4 -3. 8 -4. 1 -4. 1

2. 7 1. 3 0. 6 0. 6 3. 6

1. 8 -0. 9 -1. 7

-1. 1 -1. 8 -2. 7 -3. 0

4. 7 3. 6 1. 8 1. 3 0. 4

0. 4 5. 6 5. 6

2. 4 3. 0 6. 6 6. 6

2. 9 2. 6 1. 0 1. 0 -1. 9

-1. 9 -7. 7 -7. 7
-9. 6 -9. 6 -13. 7 -13. 7

7. 7 7. 7 6. 0 6. 0 -5. 5

-11. 9 -26. 7 -27. 4
-22. 8 -26. 4 -35. 4 -35. 6
17. 4 14. 6 8 . 7 8 . 3

T l t- 0TABLE 6 ~ 199 0 NO XEMISSIONS (10** 3 TONS )

10-5 0 BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L *TOTAL * TH E BAS E CAS E OPTIO N CAS E 5 OPTIO N CAS E 6 OPTIO N CAS E 7 NATURA L GAS AN

DOI L TH E BAS E CAS E OPTIO N CAS E 5 OPTIO N CAS E 6 01' I IO N CAS E 7 COA L TH E BAS E CAS E OPTIO N CAS E 5 OPTIO N CAS E 6 OPTIO N CAS E 7 13. 4

13. 4 13. 4 13. 4

7. 6 7. 6 7. 6 7. 6

5. 8 5. 8 5. 8 5. 8 22. 6

22. 6 22. 6 22. 6

4 . 7 4 . 7 4 . 7 4 . 7

17. 9 17. 9 17. 9 17. 9 17. 1

13. 5 11. 5 11. 5

6. 7 7. 4 8. 6 li.l,

10. 4 6. 1 2. 9 2. 9 23. 0

20. 2 14. 8 13. 7

3. 9 5. 3 8. 4 0. 9

19. 1 14. 9 6. 4 4. 8 15. 0

14. 2 9. 4 9. 4

1. 9 2. 3 4 . 8 4 . 0

13. 1 11. 9 4. 6 4. 6 42. 6

42. 7 36. 9 36. 9

6. 2 6. 2 8. 6 0. 6

36. 4 36. 5 28. 3 28. 3 133. 7

126. 6 108. 6 107. 5

30. 9 33. 6 42. 6 43. 1

102. 8 93. 0 66. 0 64. 4

T l C OTABLE 7 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MM3TU/HR ) 10-5 0 TH E BAS E CAS E OPTIO

N CAS E 5 OPTIO

N CAS E 6 OPTIO

N CAS E 7 FUEL DEMAN

D (HUMBE RO F UHITS ) NATURA L GA S AN

DOI L COA L "TOTAL * 1251 . 161 . 1412 . 1251 .

161 . 1412 . 1251 .

161 . 1412 . 1251 .

161 . 1412 . FUE L DEMAH D (10**1 2 BTUS ) HATUPA L GAS DISTILLAT E FUE

L OI L RESIDUA L FUE L OI L COA L *TOTAL * 86 . 0 . 9 . 36 . 132 . 86 .

0 . 9 . 36 . 132 . 86 .

0 . 9 . 36 . 132 . 86 .

0 . 9 . 36 . 132 . EMISSIOMS (10** 3 TOMS ) S0 2 P M HO X PMIO 68. 4 10. 9 13. 4 8. 0 68. 4

10. 9 13. 4 8. 0 68. 4

10. 9 13. 4 8. 0 68. 4

10. 9 13. 4 8. 0 EMISSIOMS l'/. CHANG

E FRO M BAS E CASE ) S0 2 F M NO X FM1 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG O AN DP M NO X FUE L •TOTAL * 651. 3 11. 5 -4. 1 664. 0 1322. 7 651. 3

11. 5 -4. 1 664. 0 1322. 7 651. 3

11. 5 -4. 1 664. 0 1322. 7 651. 3

11. 5 -4. 1 664. 0 1322. 7
ANNUALIZE

DCOST S [•/. CHANG

E FRO M BAS E CASE ) "TOTAL * 0. 0 0. 0 0. 0 0. 0 CAPITA L COST S (10»*6 . $1982 ) BOILE R FG DAN DP M NO X •TOTAL * 1524 . 31 . 30 . 1585 . 1524 .

31 . 30 . 1585 . 1524 .

31 . 30 . 1585 . 1524 .

31 . 30 . 1585 .

T lTABLE 8 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 50-7 5

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL * TH E BAS E CAS E

291 . 111 . 402 . OPTIO

N CAS E 5

291 . 111 . 402 . OPTIO

N CAS E 6

291 . 

### Ul
. 402 . OPTIO

N CAS E 7

291 . 111 . 402 . FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS . DISTILLAT E FUE

L OI L RESIDUA L FUE L OI L COA L •TOTAL * EMISSION S (10** 3 TONS ) S0 2 P M NO X PMI O EMISSION S IV. CHANG

E FRO M BAS E CASE ) S0 2 T M NO X 

## nu o ANNUALIZE

DCOST S (10**6 , $1932 ) BOILE R FG DAN DP M HO X FUE L •TOTAL * 38 . 0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

0. 0 0. 0 0. 0 0. 0

351. 5 13. 2 -2. 9 360. 1 721. 9 38 .

0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

0. 0 0. 0 0. 0 0. 0

351. 5 13. 2 -2. 9 360. 1 721. 9 38 .

0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

0. 0 0. 0 0. 0 0. 0

351. 5 13. 2 -2. 9 360. 1 721. 9 38 .

0 . 4 . 40 . 83 .

66. 4 10. 8 13. 2 7. 8

0. 0 0. 0 0. 0 0. 0

351. 5 13. 2 -2. 9 360. 1 721. 9
ANNUALIZE

DCOST S {•/. CHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 0 0. 0 0. 0 CAPITA L COST S (10*»6 , $1982 ) BOILE R FG DAN DP M NO X «TOTAL * 1084 . 34 . 10 . 1127 . 1084 .

34 . 10 . 1127 . 1084 .

34 . 10 . 1127 . 108 4

3 4 1 0 112 7

T l
CJ iTABL E 9 ~ INDUSTRIA L BOILE R NSP S NATIONAL IMPACT S B Y BOILE R SIZE , 1986-199 0

BOILE R SIZ E (MMBTU/HR ) 75-10 0 TH E BAS E CAS E OPTION

CAS E 5 OPTION

CAS E 6 OPTIO

N CAS E 7 FUE L DEMAN

D (NUMBE R OF UNITS ) NATURAL GA S AN

D OI L COAL •TOTAL * 107 . 68
. 175
. 107
.

68
. 175
. 107
.

68
. 175
. 107
.

68
. 175
. FUE L DEMAN

D (10**1 2 BTUS ) NATURAL GA S DISTILLAT E FUE L OI L RESIOUAL FUE L OI L COAL *TOTAL * 20
. 0
. 2
. 31
. 54
. 20
.

0
. 2
. 31
. 54
. 20
.

0
. 2
. 31
. 54
. 20
.

0
. 2
. 31
. 54
. EMISSION S ( 10** 3 TONS ) 50 2 PM NO X PMI O EMISSION S 17. CHANG E FRO

M BAS E CASE ) S0 2 PM NO X PMI O ANNUALIZE D C03T 9 (10*»6 , $1982 ) BOILE R FG D AN D P M NOX FUE L •TOTAL * ANNUALIZE D COST S ( X CHANGE FRO

M BAS E CASE ) •TOTAL * CAPITA L COST S (10**6 , $1982 ) BOILE R FG D AN D P M NOX •TOTAL * 54. 6 8. 6 9. 4 6. 3 54 ; 6

8. 6 9. 4 6. 3 54. 6

8. 6 9. 4 6. 3 54. 6

8. 6 9. 4 6. 3

0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0

213. 8 9. 0 -1. 9 216. 8 437. 7 213. 8

9. 0 -1. 9 216. 8 437. 7 213. 8

9. 0 -1. 9 216. 8 437. 7 213. 8

9. 0 -1. 9 216. 8 437. 7

0. 0 0. 0 0. 0 0. 0

725
. 24
. 5
. 754
. 725
.

24
. 5
. 754
. 725
.

24
. 5
. 754
. 72 5

2 4 5 75 4

T l C OTABL E 1 0 —INDUSTRIA L BOILE RNSP S NATIONAL IMPACT S BY BOILE R SIZE , 1986-199 0

BOILE R SIZ E (MMBTU/HR ) 100-15 0 TH E BAS E CA5 E OPTIO

N CAS E 5 OPTIO

N CAS E 6 OPTIO

N CAS E 7 FUE L DEMAN

D (NU'irir-* o

r UNITS ) NATURA L GA S AN DOI L COA L •TOTAL * 212 . 59 . 271 . 239 .

32 . 271 . 254 .

17 . 271 . 25 4

1 7 27 1 FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS DISTILLAT E FUE

L OI L RESIDUA L FUE L OI L COA L *TOTAL * 82 . 0 . 7 . 40 . 129 . 105 .

0 . 0 . 23 . 129 . 117 .

0 . 0 . 12 . 129 . 117 .

0 . 0 . 12 . 129 . EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMI O 74. 0 1. 8 17. 1 1. 8 U . 2

0. 9 13. 5 0. 9 2. 2

0. 8 11. 5 0. 8 1. 6

0. 8 11. 5 0. 8 EMISSION S IV. CHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMI O 0. 0 0. 0 0. 0 0. 0 -84. 9

-50. 0 -21. 1 -50. 0 -97. 0

-55. 6 -32. 7 -55. 6 -97. 8

-55. 6 -32. 7 -55. 6 ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DF M NO X FUC L *TOTAL» 354. 5 22. 6 1. 3 629. 5 1008. 0 301. 7

12. 6 -2. 5 696. 9 1008. 7 271. 0

13. 8 -3. 6 729. 0 1011. 1 270. 9

14. 7 -3. 6 729. 0 1011. 2
AHNUALIZE

DCOST S IV. CHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 O. l 0. 3 0. 3 CAPITA L COST S (10**6 , $1982 ) BOILE R FG O AM DP M HO X •TOTAL * 1196 . 79 . 20 . 1294 . 964 .

43 . 15 . 1021 . 835 .

36 . 14 . 885 . 834 .

36 . 14 . 884 .
T lTABL E 1 1 — INDUSTRIA L BOILE RNSP S NATIONA L IMPACT S B YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMDTU/HR ) 150-20 0 TH E BAS E CAS E OPTIO N

CAS E 5 OPTIO N

CAS E 6 OPTIO N

CAS E 7
FUE L DEMAND (NUMBE RO F UNITS ) NATURA L GA S ANDOI L COA L •TOTAL * 55 . 80 . 135 . 71 .

64 . 135 . 115 .

20 . 135 . 120 .

15 . 135 . FUE L DEMAND (10**1 2 BTUS ) NATURA L GA S DISTILLAT E FUE L OI L RESIDUA L FUE L OI L COA L •TOTAL * 41 . 0 . 0 . 70 . 11 . 56 .

0 . 0 . 55 . U l . 88 .

0 . 0 . 23 . U l . 94 .

0 . 0 . 17 . U l . EMISSION S ( 10** 3 TONS ) • S0 2 P M HO X PMI O
EMISSION S I.V. CHANG E FROM

BAS E CASE ) S0 2 P M HO X PMI O
ANNUALIZE DCQST S (10**6 , $1902 ) COILE R ronAM DP M HO X 

### run . •TOTAL *
AHMUALIZE DCOST S IV. CHANG E FROM

BAS E CASE ) •TOTAL *
CAPITA L COST S (10**6 , $1902 ) BOILE R FGDANDP

M NO X •TOTAL * 107. 8 1. 3 23. 0 1. 2 25. 9

1. 1 20. 2 1. 1 4. 0

0. 8 14. 8 0. 8 2. 3

0. 7 13. 7 0. 7

0. 0 0. 0 0. 0 0. 0 -76. 0

-15. 4 -12. 2 -8. 3 -96. 3

-38. 5 -35. 7 -33. 3 -97. 9

-46. 2 -40. 4 -41. 7

365. 9 40 . ?. 3. 6 4P7.* > 837. 6 320. 2

31. 9 1. 8 tni . | 043. 1 221. 4

?.?..n -0. 9 i-.*v>. 7 032. 9 204. 6

JO.f t -1. 7 f.07. 7 829. 4

0. 0 0. 7 -0. 6 •1. 0

1369 . 140 . 12 . 1521 . 1173 .

112 . 12 . 1297 . 714 .

53 . 11 . 778 . 646 .

40 . 11 . 697 .

T l
0 0TABLE 1 2 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 200-25 0 TH E BAS E CAS E ,OPTIO

N CAS E 5 OPTIO

N CAS E 6 OPTIO

N CAS E 7 FUE L DEMAH D (NUMBE RO F UNITS ) NATURA L GA S AN DOI L COA L "TOTAL * 21 . 41 . 62 . 26 .

36 . 62 . 49 .

13 . 62 . 4 9

1 3 6 2 FUE L DEMAN D ( 10**1 2 BTUS ) NATURA L GAS DISTILLAT E FUE

L OI L RESIDUA L FUEL OI L COA L •TOTAL * 19 . 0 . 0 . 48 . 67 . 24 .

0 . 0 . 43 . 67 . 50 .

0 . 0 . 17 . 67 . 50 .

0 . 0 . 17 . 67 . EMISSION S (10** 3 TONS ) 50 2 P M NO X PMI O 05. 5 0. 8 15. 0 0. 8 19. 7

0. 8 14. 2 0. 8 3. 0

0. 5 9. 4 0. 5 2. 4

0. 5 9. 4 0. 5 EMISSIONS ( Z CHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMI O 0. 0 0. 0 0. 0 0. 0 -77. 0

0. 0 -5. 3 0. 0 -96. 5

-37. 5 -37. 3 -37. 5 -97. 2

-37. 5 -37. 3 -37. 5 AHNUALIZE

O COST S (10*"6 , $1932 ) BOILE R FG DAN DP M NO X FUE L •TOTAL * 223. 7 26. 4 0. 4 242. 5 493. 1 209. 6

23. 6 -0. 4 271. 6 504. 4 142. 0

18. 1 -5. 6 346. 5 501. 1 141. 9

19. 2 -5. 6 345. 6 501. 1
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 2. 3 1. 6 1. 6
CAPITA L COST S (10**6 , $1982 ) BOILE R FG DAN DP M HO X •TOTAL * 824 . 68 . 8 . 920 . 754 .

77 . 8 . 839 . 446 .

41 . 8 . 495 . 44 6

4 1 8 49 5

T l C OTABLE 1 3 ~ INDUSTRIA L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 25 0 THE BAS E CAS E OPTIO

N CAS E 5 OPTIO

N CAS E 6 OPTIO

N CAS E 7 FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L *TOTAL» 70 . 66 . 136 . 70 .

66 . 136 . 86 .

50 . 136 . 8 6

5 0 13 6 FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS DISTILLAT E FUEL OI L RESIOUA L FUEL OI L COA L •TOTAL * 65 . 0 . 0 . 126 . 191 . 65 .

0 . 0 . 126 . 191 . 90 .

0 . 0 . 101 . 191 . 90 .

0 . 0 . 101 . 191 . EMISSIONS (10** 3 TONS )

. 50 2 P M NO X PMI O 58. 6
k
. • C 42. 6 2. 2 56. 5

42. 7 2. 2 17. 0

1. 9 36. 9 1. 9 9. 7

1. 9 36. 9 1. 9 EMISSIONS IV. CHANG

E FRO M BAS E CASE ) S0 2 F M HO X FM1 0 0. 0 0. 0 0. 0 0. 0 -3. 6

0. 0 0. 2 0. 0 -71. 0

-13. 6 -13. 4 -13. 6 -83. 4

-13. 6 -13. 4 -13. 6
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG O AM DP M NO X FUE L •TOTAL * 558. 2 63. 0 -1. 9 767. 1 1386. 3 558. 2

62. 9 -1. 9 767. 4 1306. 7 496. 2

87. 6 -7. 7 838. 5 1414. 6 494. 1

89. 6 -7. 7 838. 9 1415. 0
ANNUALIZE

DCOST S IV. CHANG

E FRO M BAS E CASE ) *TOTAL * 0. 0 0. 0 2. 0 2. 1 CAPITA L COST S (10**6 , $1982 ) BOILE R FG DMID P M NO X •TOTAL * 1981 . 188 . 20 . 2189 . 1981 .

187 . 20 . 2189 . 1696 .

207 . 20 . 1922 . 1684 .

206 . 20 . 1909 .

T l h o oTABLE 1 4 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 10 0 TH E DAS E CAS E OPTIO

N CAS E 5 OPTIO

N CAS E 6 OPTIO

N CAS E 7 FUE L DEMAN D (HUMME R01 " UNITS ) NA1URA L GAS AN

DOI L COA L »TOTAL * 350 . 246 . 604 . 406 .

190 . 604 . 504 .

100 . 604 . 509 .

95 . 604 . FUEL DEMAN

D (10**1 2 BTUS ) NATURA L GA S DISTILLAT E FUE

L OI L RESIOUA L FUE L OI L COA L •TOTAL * 207 . 0 . 7 . 284 . 498 . 250 .

0 . 0 . 248 . 498 . 345 .

0 . 0 . 153 . 498 . 351 .

0 . 0 . 147 . 498 . EMISSION S (10«i* 3 TONS ) 50 2 I' M HO X PMI O 25. 9 6. 1 97. 7 6. 0 113. 3

5. 0 90. 6 5. 0 26. 2

4. 0 72. 6 4. 0 16. 0

3. 9 71. 5 3. 9 EMISSIOMS ( XCHANG

E FRO M DAS E CASE ) S0 2 P M NO X PMI O 0. 0 0. 0 0. 0 0. 0 -65. 2

-10. 0 -7. 3 -16. 7 -92. 0

-34. 4 -25. 7 -33. 3 -95. 1

-36. 1 -26. 8 -35. 0
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN O P M NO X FUE L •TOTAL * 1502. 4 152. 2 3. 4 2067. 0 3725. 1 1389. 6

131. 1 -2. 9 2225. 1 3742. 9 1130. 6

142. 3 -17. 7 2504. 5 3759. 7 1111. 6

142. 3 -18. 5 2521. 2 3756. 7 ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 5 0. 9 0. 8 CAPITA L COST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X *TOTAL» 5371 . 494 . 60 . 5925 . 4872 .

419 . 54 . 5345 . 3691 .

336 . 53 . 4080 . 3610 .

323 . 53 . 3986 .

T lTABL E 1 5 INDUSTRIA L BOILE R NSP S NATIONAL IMPACT S BY BOILE R SIZE , 1986-199 0

BOILE R SIZ E 100-25 0 (MMBTU/HR )

FUE L DEMAN

D (NUMBE R O

F UNITS ) NATURA L GA S AN

D OI L COA L •TOTAL * TH E BAS E OPTIONOPTIO H OPTIO H CAS E CAS E 5 CAS E 6 CAS E 7

288
. 180
. 468
. 336
.

132
. 468
. 418
.

5 0
. 468
. 4 2 3

4 5 4 6 8 FUE L DEMAHD (10**1 2 BTUS ) NATURAL GA S DISTILLAT E FUE L OI L PESIDUA L FUE L OI L COA L •TOTAL * 142

. 0

. 7

. 158

. 307 . 185

.

0

. 0

. 122

. 307

. 255

.

0

. 0

. 5 2

. 307 . 261

.

0

. 0

. 4 6

. 307 . EMISSION S ( 10** 3 TONS ) 50 2 F M NOX FM1 0 267. 3 3 . 9 55. 1 3 . 8 56. 8

2 . 8 47. 9 2 . 8 9 . 2

2 . 1 35. 7 2 . 1 6 . 3

2 . 0 34. 6 2 . 0 EMISSION S ( X CHANGE FRO

M BAS E CASE ) S0 2 F M HOX PMI O AHNUALIZE D COST S (10"**6
. $1902 ) BOILE R FG D AH D PM HOX FUE L «I(IIAL« 0 . 0 0 . 0 0 . 0 0 . 0 -78. 8

-28. 2 -13. 1 -26. 3 -96. 6

-46. 2 -35. 2 -44. 7 -97. 6

-48. 7 -37. 2 -47. 4

944. 2 89. 2 5 . 3 1299. 9 Clin. 7 831. 5

68. 1 -1. 1 1457. 7 rar.A. c 634. 4

54. 8 -10. 1 1666. 0 PVin. l 617. 5

52. 7 -10. 8 1682. 3 [HI, ?
AHHUALIZE D COST S ( X CHANG E FRO

M BAS E CASE ) •TOTAL * 0. 0 0. 7 0. 3 0. 1
CAPITA L COST S (10**6 , $1902 ) POILE R FG D AN D P M HOX •TOTAL * 3390

. 306

. 4 0

. 3735

. 2891

.

231

. 3 4

. 3157

. 1995

.

129

. 3 3

. 2158

. 192 6

11 7 3 3 207 7TABLE 1 6 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MM3TU/HR ) > 5 0 TH E BAS E CAS E OPTIO

N CAS E 5 OPTIO

N CAS E 6 OPTIO

N CAS E 7 FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL * 756 . 425 . 1181 . 804 .

377 . 1181 . 902 .

279 . 1181 . 907 .

274 . 1181 . FUE L DEMAN D ( 10**1 2 BTUS ) NATURA L GAS DISTILLAT E FUE

L OI L RESIDUA L FUE L OI L COA L •TOTAL * 266 . 0 . 13 . 355 . 634 . 309 .

0 . 6 . 319 . 634 . 404 .

0 . 6 . 225 . 634 . 410 .

0 . 6 . 219 . 634 . EMISSION S ( 10«* 3 TONS ) 50 2 P M NO X PMIO 446. 9 25. 5 120. 3 20. 1 234. 3

24. 4 113. 2 19. 1 147. 2

23. 4 95. 2 18. 1 137. 0

23. 3 94. 1 18. 0 EMISSION S ( XCHANG

E FRO M BAS E CASE ) S0 2 F M MO X PMIO 0. 0 0. 0 0. 0 0. 0 -47. 6

-4. 3 -5. 9 -5. 0 -67. 1

-8. 2 -20. 9 -10. 0 -69. 3

-8. 6 -21. 8 -10. 4
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN O P H NO X FUE L •TOTAL * 2067. 8 174. 4 -1. 4 2643. 9 4884. 6 1955. 0

153. 2 -7. 8 2802. 0 4902. 5 1696. 0

164. 5 -22. 6 3081. 3 4919. 2 1677. 0

164. 5 -23. 3 3093. 1 4916. 2
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 4 0. 7 0. 6 CAPITA L COST S (10**6 , $1982 ) BOILE R FG DAN DP M HO X •TOTAL * 7179 . 552 . 75 . 7806 . 6681 .

477 . 69 . 7226 . 5499 .

394 . 68 . 5961 . 5418 .

381 . 68 . 5867 .TABLE 1 7 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) TOTA L TH E BAS E OPTIO

N OPTIO

N OPTIO

N CAS E CAS E 5 CAS E 6 CAS E 7 FUEL DEMAH

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL * 2007 . 2055 . 586 . 538 . 2593 . 2593 . 2153 . 2158 . 440 . 435 . 2593 . 2593 . FUE L DEMAN D ( 10**1 2 BTUS ) NATURA L GAS • DISTILLAT E FUEL OI L RESIDUA L FUE L OI L COA L •TOTAL * 352 . 0 . 22 . 392 . 766 . 396 .

0 . 15 . 356 . 766 . 490 .

0 . 15 . 261 . 766 . 496 .

0 . 15 . 255 . 766 . EMISSION S (10** 3 TONS ) S0 2 P M NO X PMI O 515. 2 36. 4 133. 7 28. 2 302. 7

35. 2 126. 6 27. 1 215. 6

34. 2 108. 6 26. 1 205. 3

34. 2 107. 5 26. 0 EMISSION S ( XCHANG

E FRO M BAS E CASE ) S0 2 P M HO X PMI O 0. 0 0. 0 0. 0 0. 0 -41. 2

-3. 3 -5. 3 -3. 9 -58. 2

-6. 0 -18. 8 -7. 4 -60. 2

-6. 0 -19. 6 -7. 8
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L •TOTAL * 2719. 1 185. 9 -5. 5 3307. 9 6207. 3 2606. 3

164. 7 -11. 9 3466. 0 6225. 2 2347. 3

176. 0 -26. 7 3745. 3 6241. 9 2328. 3

176. 0 -27. 4 3762. 1 6239. 0
ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 3 0. 6 0. 5 CAPITA L COST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X *TOTAL» 8703 . 583 . 105 . 9391 . 8205 .

507 . 99 . 8811 . 7024 .

425 . 98 . 7546 . 694 3

41 2 9 8 745 2