p. 1



# OAR Box

# 1828 Prepped byOllie Stewart



# Document

Number: 

# 281 ) ll-K-(I)-9 4

Docket Number: 

# A-83-2 7

Printed 11/12/200811:12:58AM Sheet 281 of 325

# ;* T

199 0 PROJECTE DNE UINDUSTRIALFOSSI LFUEL-FIRE DBOILE R

AI REMISSIONS , FUE LDEMAND , AN DCOST S

NOTE S ON

IFCA M PROJECTION S (REFERENC ECAS EFUE LPRICES )

PREPARE DFOR :
TH EU.S . ENVIRONMENTALPROTECTION AGENCY

PREPARE DBY : ENERGYANDENVIRONMENTALANALYSIS , INC . 165 5 NORT HFOR T MYERDRIVE ARLINGTON , VIRGINI A 2220 9 11/05/8 4

I I

i —i I t oNOTE S ON IFCA M PROJECTION S **************************

1 . SUMMARYOF SEVE N SELECTE D( A

SUBSE T O F THE ) FIFT HROUND S0 2 NSP S IFCA

M RUN S
2 . BAS E CAS E

- S02 : CURREN T NSP S

- PM : PROPOSE DNSP S (4 9 F R25103 )

- NOX : LE

A O RSCA REQUIRE O( > 10 0 MMBTU/HR )
3 . OPTION

CAS E 1

- COMPLIANC E FUEL S (100-25 0 MMBTU/HR) : 1.67. S RESI DAN D 1. 7 LBS02/MMBT UCOA L

- COMPLIANC E FUELS ( >25 0 MMBTU/HR) : 0.8/ C S RESI DAN

D 1. 2 LBS02/MMBT UCOA L

- NON-COMPLIANC E FUELS : MI N 505 * S0 2 REOUCTION UIT H 0. 9 LBS02/MMBT UCEILING
4 . OPTION

CAS E 2

- COMPLIANC E FUELS : 0.6J JS RESI DAN

D1. 2 LBS02/MMBT U

- NON-COMPLIANC E FUELS : SAME A S O.C . 1
5 . OPTION

CAS E 3

- COMPLIANC E FUELS : 0.8/ C S RESI D

- NON-COMPLIANC E FUELS : SAME A S O.C . 1
6 . OPTION

CAS E 4

- COMPLIANC E FUELS : 0.3 XS RESI D

- NON-COMPLIANC E FUELS : 0. 6 LBS02/MMBT UCEILING
7 . OPTION

CAS E 5

- COMPLIANC E FUELS : 0.3/ C S RESI D

- NON-COMPLIANC E FUELS : CURREN T ELECTRI C UTILIT YNSP S
6 . OPTION

CAS E 6

- NOCOMPLIANC E RESI DO RCOA LTYPE S

- NON-COMPLIANC E FUELS : 90 * S0 2 REDUCTION

T J C OP. 4

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### o ro OTC LZINDUSTRIALBOILE RNE USOURC E PERFORMANC E STANDARD S ASSUMPTION S OPTION CAS E 2 (AR013 2 )

NATURAL GA S S0 2 CEILING(LB/MMBTU ) PM CEILING(LB/MMBTU ) NO XCEILING(LB/MMBTU )

DISTILLAT E FUE L OI L S0 2 CEILING(LB/MMBTU ) PM CEILING(LB/MMBTU ) NO XCEILING(LB/MMBTU )

RESIDUA L FUE L OI L S0 2 CEILING(LB/MMBTU ) PM CEILING(LB/MMBTU ) NO XCEILING(LB/MMBTU )

COA L S0 2 CEILING(LB/MMBTU ) PM CEILING(LB/MMBTU )

- FOR<30 XC U NO XCEILING(LB/MMBTU ) 10-3 0 BOILE RSIZ E CATEGORY(MMBTU/H RHEA T INPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E

NON E NON E NON E

NON E NON E . NON E

NON E NON E NON E NON E NONE

NONE 0.2 0

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0.9 0 NON E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NON E

NON E 0.2 0

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0.9 0 NON E 0.3 1

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NON E 0.2 0

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NON E 0.3 0

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0.9 0 0.0 5 0.0 5 0.7 0

MANDATORYSCRUBBINGREGULATION S
RESIOUAL FUE L OI L S0 2 FLOOR(LB/MMBTU ) PERCEN T S0 2 REMOVAL REQUIRE D MINIMUM

PERCEN T S0 2 REMOVALREQUIRE D LOUSULFUREXEMPTION (L BS02/MMBTU )

COAL S0 2 FLOOR(LB/MMBTU ) PERCEN T S0 2 REMOVAL REQUIRE D MINIMUM

PERCEN T SO 2 REMOVALREQUIRE D LOUSULFUREXEMPTION (L BS02/MMBTU ) NON E NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON E

50.0 0 NONE 0.8 5

NONE 50.0 0 NONE 1.2 0 NON E

50.0 0 NON E 0.8 5

NON E 50.0 0 NON E 1.2 0 NON E

50.0 0 NON E 0.8 5

NON E 50.0 0 NON E 1.2 0 NON E

50.0 0 NON E 0.6 5

NON E 50.0 0 NON E 1.2 0INDUSTRIA L BOILE RNE USOURCE PERFORMANC E STANDARDS ASSUMPTIONS OPTIO N CAS E 3 (AR013 3 )

NATURA LGAS S0 2 CEILIN

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

G(LB/MMBTU )
DISTILLATE FUELOI L S0 2 CEILIN

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

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

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

G(LB/MMBTU )
COA L S0 2 CEILIN

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

- FO R<30 XC

U NO XCEILIN

G(LB/MMBTU ) 10-3 0 BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )
30-5 0 50-7 5 75-10 0 100-15 0 150-20 0 200-25 0 >25 0

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E

NON E NON E NON E

NON E NON E . NON E

NON E NON E NON E NON E NON

E NON E 0.2 0

NON E NON E 0.2 0

0.9 0 NON E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NON

E NON E 0.2 0

NON E NON E 0.2 0

0.9 0 NON E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NON

E NON E 0.2 0

NON E NON E 0.2 0

0.9 0 NON E 0.3 1

0.9 0 0.0 5 0.2 0 0.6 0 NON

E NON E 0.3 0

NON E 0.1 0 0.3 0

0.9 0 0.1 0 0.3 1

0.9 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIN

GREGULATIONS
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

LREQUIRE

D LO USULFU REXEMPTIO

N (L BS02/MMBTU )
COA L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

N (L BS02/MMBTU ) NON E NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E NON

E 50.0 0 NON E 0.8 5

NON E 50.0 0 NON E NON E NON

E 50.0 0 NON E 0.8 5

NON E 50.0 0 NON E NON E NON

E 50.0 0 NON E 0.8 5

NON E 50.0 0 NON E NON E NON

E 50.0 0 NON E 0.8 5

NON E 50.0 0 NON E NON EP. 7

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

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

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Y(MMBTU/H

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NON E NON E NON E

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NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E

NON E NON E NON E

NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E

NON E NON E NON E

NON E NON E . NON E

NON E NON E NON E NON E NON

E NON E 0.2 0

NON E NON E 0.2 0

1.2 0 NON E 0.3 1

1.2 0 0.0 5 0.2 0 0.6 0 NON

E NON E 0.2 0

NON E NON E 0.2 0

1.2 0 NON E 0.3 1

1.2 0 0.0 5 0.2 0 0.6 0 NON

E NON E 0.2 0

NON E NON E 0.2 0

1.2 0 NON E 0.3 1

1.2 0 0.0 5 0.2 0 0.6 0 NON

E NON E 0.3 0

NON E 0.1 0 0.3 0

1.2 0 0.1 0 0.3 1

1.2 0 0.0 5 0.0 5 0.7 0

MANDATOR

YSCRUBBIN

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RESIOUA LFUE LOI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

LREQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

D LO USULFU REXEMPTIO

N (L BS02/MMBTU )
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L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

LREQUIRE

O LO USULFU REXEMPTIO

N (L BS02/MMBTU ) NON E NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E NON

E NON E NON E NON E

NON E NON E NON E NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON E 0.6 0 90.0 0 70.0 0 0.3 5

0.6 0 90.0 0 70.0 0 NON E

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2^ rOTLIST O F TABLE S

DESCRIPTIO

N O F TABL E TABLE NUMBE R

FUE LDEMAN D

- NUMBE RO F UNIT S 1

- BTUS O

F FUE LCONSUMPTIO

N 2
POLLUTAN

T EMISSIONS 3
COST S 4
NO XONL Y

- CONTRO

LCOST S 5

- EMISSIONS 6 NATIONA LIMPACT 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 11

- 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

REGIONA L IMPACT S

- S0 2 EMISSIONS 100-15 0 MMBTU/H

R1 8 150-20 0 MMBTU/H

R1 9 200-25 0 MMBTU/H

R2 0 > 25 0 MMBTU/H

R2 1

- FOSSI LFUE

LDEMAN D 100-15 0 MMBTU/H

R2 2 150-20 0 MMBTU/H

R2 3 200-25 0 MMBTU/H

R2 4 > 25 0 MMBTU/H

R2 5

- ANNUALIZE

DCOST S 100-15 0 MMBTU/H

R2 6 150-20 0 MMBTU/H

R2 7 200-25 0 MMBTU/H

R2 8 > 25 0 MMBTU/H

R2 9TABL E 1 ~ 199 0 FUE

L DEMAN D (NUMBE RO F UNITS )

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 OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NATURA L GA S TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
COA L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N CAS E CAS E CAS E CAS E CAS E CAS E CAS E 1 2 3 4 5 6
AN DOI L 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 1 2 3 4 5 6

1 2 3 4 5 6 141 2 141 2 141 2 141 2 141 2 141 2 141 2

139 8 139 8 139 8 139 8 139 8 139 8 139 8

1 4 1 4 1 4 1 4 1 4 1 4 1 4 577 .

577 . 577 . 577 . 577 . 577 . 577 .

556 . 556 . 556 . 556 . 556 . 556 . 556 .

21 . 21 . 21 . 21 . 21 . 21 . 21 . 271 .

271 . 271 . 271 . 271 . 271 . 271 .

265 . 267 . 267 . 270 . 271 . 271 . 271 .

6 . 4 . 4 . 1 . 0 . 0 . 0 . 135 .

135 . 135 . 135 . 135 . 135 . 135 .

134 . 134 . 134 . 135 . 135 . 135 . 135 . 62 .

62 . 62 . 62 . 62 . 62 . 62 .

58 . 62 . 62 . 62 . 62 . 62 . 62 .

4 . 0 . 0 . 0 . 0 . 0 . 0 . 136 .

136 . 136 . 136 . 136 . 136 . 136 .

130 . 130 . 130 . 132 . 129 . 124 . 124 .

6 .ff6 . 4 . 7 . 12 . 12 . 259 3

259 3 259 3 259 3 259 3 259 3 259 3

254 1 254 7 254 7 255 3 255 1 254 6 254 6

5 2 4 6 4 6 4 0 4 2 4 7 4 7TABL E 2 « 199 0 FUE

L DEMAN D (10**1 2 BTUS )

10-5 0 BOILE

RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L

TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NATURA L GA S TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N CAS E CAS E 1 CAS E 2 CAS E 3 CAS E 4 CAS E 5 CAS E 6

CAS E CAS E 1 CAS E 2 CAS E 3 CAS E 4 CAS E 5 CAS E 6
RESIDUA L FUE L OI L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
COA L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N CAS E CAS E 1 CAS E 2 CAS E 3 CAS E 4 CAS E 5 CAS E 6

CAS E CAS E 1 CAS E 2 CAS E 3 CAS E 4 CAS E 5 CAS E 6 132 .

132 . 132 . 132 . 132 . 132 ; 132 .

34 . 34 . 34 . 34 . 34 . 3* . 34 .

94 . 94 . 94 . 94 . 94 . 94 . 94 .

4 . 4 . 4 . 4 . 4 . 4 . 4 . 136 .

136 . 136 . 136 . 136 . 136 . 136 .

26 . 26 . 26 . 26 . 26 . 26 . 26 .

101 . 101 . 101 . 101 . 101 . 101 . 101 .

8 . 8 . 8 . 6 . 8 . 6 . 8 . 129 .

129 . 129 . 129 . 129 . 129 . 129 .

26 . 26 . 56 . 58 . 72 . 72 . 65 .

99 . 100 . 70 . 70 . 57 . 57 . 44 . 24 .

24 . 50 . 51 . 54 . 54 . 60 .

86 . 86 . 60 . 60 . 57 . 57 . 51 .

1 . 1 . 1 . 0 . 0 . 0 . 0 . 67 .

67 . 67 . 67 . 67 . 67 . 67 .

15 . 16 . 33 . 33 . 34 . 34 . 35 .

46 . 51 . 34 . 34 . 33 . 33 . 32 . 191 .

191 . 191 . 191 . 191 . 191 . 191 .

87 . 87 . 87 . 91 . 107 . 107 . 113 .

92 . 92 . 92 . 92 . 70 . 59 . 52 .

13 . 13 . 13 . 9 . 15 . 26 . 26 . 766 .

766 . 766 . 766 . 766 . 766 . 766 .

212 . 213 . 286 . 293 . 328 . 328 . 355 .

518 . 524 . 452 . 452 . 411 . 401 . 374 .

35 . 28 . 28 . 21 . 27 . 37 . 37 .TABLE 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 OPTIO N OPTIO N OPTIO N
P M TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NO X TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
PMIO TH E BAS E OPTIO N OPTIO N OPTIO N 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 CAS E CAS E CAS E CAS E CAS E

CAS E CAS E CAS E CAS E CAS E CAS E CAS E 1 2 3 4 5 6

1 2 3 4 5 6

1 2 3 4 5 6

1 2 3 4 5 6 107 .

107 . 107 . 107 . 107 . 107 . 107 .

10 . 10 . 10 . 10 . 10 . 10 . 10 .

19 . 19 . 19 . 19 . 19 . 19 . 19 . 114 .

114 . 114 . 114 . 114 . 114 . 114 .

10 . 10 . 10 . 10 . 10 . 10 . 10 .

21 . 21 . 21 . 21 . 21 . 21 . 21 .

10 . 10 . 10 . 10 . 10 . 10 . 10 . 105 .

70 . 28 . 27 . 15 . 13 . 4 .

8 . 6 . 4 . 4 . 3 . 3 . 3 .

15 . 16 . 13 . 12 . 13 . 13 . 13 .

8 . 6 . 4 . 4 . 3 . 3 . 3 . 82 .

60 . 24 . 23 . 16 . 13 . 4 .

7 . 5 . 3 . 3 . 4 . 4 . 4 .

14 . 15 . 12 . 12 . 13 . 13 . 13 .

7 . 5 . 3 . 3 . 4 . 4 . 4 . 52 .

35 . 14 . 14 . 9 . 8 . 3 .

4 . 3 . 2 . 2 . 2 . 2 . 2 .

9 . 9 . 8 . 8 . 8 . 8 . 8 .

4 . 3 . 2 . 2 . 2 . 2 . 2 . 41 .

40 . 40 . 38 . 17 . 13 . 6 .

4 . 4 . 4 . 4 . 3 . 3 . 3 .

21 . 21 . 21 . 20 . 21 . 23 . 23 .

4 . 4 . 4 . 4 . 3 . 3 . 3 . 50 0

42 6 32 7 32 2 27 8 26 8 23 7

4 2 3 9 3 3 3 3 3 3 3 2 3 2

9 9 10 0 9 3 9 1 9 4 9 6 9 6

4 1 3 8 3 2 3 2 3 2 3 1 3 1IUALIZE DCOST S TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E
•ITA L COST S TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E _ 1 2 3 4 5 6

-
1 2 3 4 5 6 10-5 0
TOTA L 1215. 4 1215. 4 1215. 4 1215. 4 1215. 4 1215. 4 1215. 4
TOTA L 1290. 1 1290. 1 1290. 1 1290. 1 1290. 1 1290. 1 1290. 1 TABL

E 4 — 199 0 COST S (10**6 , $1982 )
BOILE RSIZ E 50-10 0

1041. 9 1041. 9 1041. 9 1041. 9 1041. 9 1041. 9 1041. 9

1154. 3 1154. 3 1154. 3 1154. 3 1154. 3 1154. 3 1154. 3 100-15 0

900. 9 905. 6 926. 2 927. 0 941. 8 941. 9 944. 7

. 812. 6 776. 2 778. 7 749. 7 765. 1 763. 4 763. 7 (MMBTU/HR )

150-20 0

728. 5 732. 8 749. 3 749. 2 760. 7 761. 2 763. 0

511. 5 501. 5 501. 4 485. 7 513. 8 514. 0 511. 5 200-25 0

445. 3 443. 7 455. 6 455. 6 459. 5 459. 8 460. 8

359. 4 285. 3 293. 7 293. 7 301. 4 301. 5 301. 0 > 25 0

1274. 6 1274. 7 1274. 7 1275. 9 1307. 2 1310. 9 1313. 2

904. 8 904. 9 904. 9 861. 6 961. 8 1073. 5 1076. 8 TOTA

L

5606. 6 5614. 1 5663. 2 5665. 0 5726. 4 5731. 2 5739. 0

5032. 7 4912. 2 4923. 1 4835. 2 4986. 5 5096. 7 5097. 4

T JTABL E 5 ~ 199 0 NO

XCONTRO

L ANNUALIZE

DCOST S (10**6 , $1982 )

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 OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
NATURA L GA S TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N
COA L TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N CAS E CAS E 1 CAS E 2 CAS E 3 CAS E 4 CAS E 5 CAS E 6
AN DOI L CAS E CAS E 1 CAS E 2 CAS E 3 CAS E 4 CAS E 5 CAS E 6

CAS E CAS E 1 CAS E 2 CAS E 3 CAS E 4 CAS E 5 CAS E 6 -2. 3

-2. 3 -2. 3 -2. 3 -2. 3 -2. 3 -2. 3

-2. 3 -2. 3 -2. 3 -2. 3 -2. 3 -2. 3 -2. 3

0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 -5. 2

-5. 2 -5. 2 -5. 2 -5. 2 -5. 2 -5. 2

0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 8. 0

-0. 1 -1. 2 -1. 4 -1. 6 -1. 6 -1. 9

7. 8 -0. 3 -1. 4 -1. 4 -1. 6 -1. 6 -1. 9

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

-0. 2 -1. 1 -1. 3 -0. 9 -0. 9 -1. 1

.4. 9 -0. 3 -1. 2

-1. 1

0. 1 0. 1 0. 1 0. 0 0. 0 0. 0 0. 0 1. 1

5. 1 6. 0 6. 0 5. 6 5. 6 5. 7

1. 5 5. 1 6. 0 6. 0 5. 6 5. 6 5. 7

0. 4 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 -19. 9

-19. 9 -19. 9 -20. 7 -20. 4 -16. 6 -18. 8

-20. 6 -20. 6 -20. 6 -21. 2 -21. 2 -20. 0 -20. 3

0. 7 0. 7 0. 7 0. 5 0. 8 1. 4 1. 4 -15. 7

-32. 8 -35. 8 -36. 9 -36. 1 -34. 4 -35. 0

-17. 1 -33. 7 -36. 8 -37. 4 -36. 9 -35. 8 -36. 5

1. 4 0. 9 0. 9 0. 5 0. 8 1. 4 1. 4TABL E 6 —199 0 NO XEMISSION S (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 OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N

NATURAL GA S TH E BAS E OPTIO N OPTIO N OPTIO N OPTIO N OPTIO N OPTION
COA L TH E BAS E OPTIO N OPTION OPTION OPTION OPTION OPTION CAS E

CAS E CAS E CAS E CAS E CAS E CAS E 1 2 3 4 5 6

ANDOI L 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 1 2 3 4 5 6

1 2 3 4 5 6 16. 8

18. 8 18. 8 18. 8 18. 8 18. 8 18. 8

18. 2 18. 2 18. 2 18. 2 18. 2 18. 2 18. 2

0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 0. 6 20. 8

20. 8 20. 8 20. 8 20. 8 20. 8 20. 8

18. 7 18. 7 18. 7 18. 7 18. 7 18. 7 18. 7

2. 1 2. 1 2. 1 2. 1 2. 1 2. 1 2. 1 15. 2

16. 2 12. 5 12. 2 12. 6 12. 6 12. 6

14. 1 15. 5 11. 8 12. 0 12. 6 12. 6 12. 6

1. 1 0. 7 0. 7 0. 2 0. 0 0. 0 0. 0 13. 6

14. 6 12. 0 11. 8 12. 9 12. 9 12. 9

13. 3 14. 3 11. 7 11. 8 12. 9 12. 9 12. 9

0. 3 0. 3 0. 3 0. 0 0. 0 0. 0 0. 0 9. 4

8. 9 7. 8 7. 8 8. 0 8. 0 8. 0

7. 8 8. 9 7. 8 7. 8 8. 0 8. 0 8. 0

1. 6 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 20. 8

20. 8 20. 8 20. 0 20. 9 22. 9 23. 1

17. 2 17. 2 17. 2 17. 6 16. 7 15. 7 15. 9

3. 6 3. 6 3. 6 2. 4 4. 2 7. 2 7. 2 98. 6

100. 0 92. 7 91. 3 94. 1 9fr. O 96. 1

89. 4 92. 7 85. 4 86. 1 87. 3 86. 2 86. 3

9. 2 7. 3 7. 3 5. 2 6. 8 9. 6 9. 8TABLE 7 INDUSTRIA LBOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 10-5 0

FUELDEMAN

D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L •TOTAL *
FUELDEMAN

D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUEL OI L RESIDUA LFUE LOI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E S0 2 P M NO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L •TOTAL * FRO M BAS E CASE ) TH E BAS E CAS E

1398 . 14 . 1412 .

34 . 0 . 94 . 4 . 132 .

107. 2 9. 5 18. 8 9. 0

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

571. 2 1. 8 -2. 3 644. 7 1215. 4 OPTIO

N CAS E 1

1398 . 14 . 1412 .

34 . 0 . 94 . 4 . 132 .

107. 2 9. 5 18. 8 9. 0

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

571. 2 1. 8 -2. 3 644. 7 1215. 4 OPTIO

N CAS E 2

1398 . 14 . 1412 .

34 . 0 . 94 . 4 . 132 .

107. 2 9. 5 18. 8 9. 0

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

571. 2 1. 8 -2. 3 644. 7 1215. 4 OPTIO

N CAS E 3

1398 . 14 . 1412 .

34 . 0 . 94 . 4 . 132 .

107. 2 9. 5 18. 8 9. 0

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

571. 2 1. 8 -2. 3 644. 7 1215. 4 OPTIO

N CAS E 4

1398 . 14 . 1412 .

34 . 0 . 94 . 4 . 132 .

107. 2 9. 5 18. 8 9. 0

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

571. 2 1. 8 -2. 3 644. 7 1215. 4 OPTIO

N CAS E 5

1398 . 14 . 1412 .

34 . 0 . 94 . 4 . 132 .

107. 2 9. 5 18. 8 9. 0

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

571. 2 1. 8 -2. 3 644. 7 1215. 4 OPTIO

N CAS E 6

1398 . 14 . 1412 .

34 . 0 . 94 . 4 . 132 .

107. 2 9. 5 18. 8 9. 0

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

571. 2 1. 8 -2. 3 644. 7 1215. 4
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0
CAPITA L COST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X *TOTAL» 1255 . 4 . 31 . 1290 . 1255 .

4 . 31 . 1290 . 1255 .

4 . 31 . 1290 . 1255 .

4 . 31 . 1290 . 1255 .

4 . 31 . 1290 . 1255 .

4 . 31 . 1290 . 1255 .

4 . 31 . 1290 .TABL E 8 — INDUSTRIA

L BOILE RNSP S NATIONA

LIMPACT 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»
FUEL DEMAN

D (10**1 2 BTUS ) NATURA L GAS DISTILLATE FUE

L OI L RESIDUA L FUE L OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO \ ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L •TOTAL * TH E BAS E CAS E

390 . 12 . 402 .

16 . 0 . 62 . 4 . 83 .

70. 2 6. 1 12. 7 5. 9

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

251. 1 3. 9 -3. 1 395. 6 647. 5 OPTIO

N CAS E 1

390 . 12 . 402 .

16 . 0 . 62 . 4 . 83 .

70. 2 6. 1 12. 7 5. 9

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

251. 1 3. 9 -3. 1 395. 6 647. 5 OPTIO

N CAS E 2

390 . 12 . 402 .

16 . 0 . 62 . 4 . 83 .

70. 2 6. 1 12. 7 5. 9

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

251. 1 3. 9 -3. 1 395. 6 647. 5 OPTIO

N CAS E 3

390 . 12 . 402 .

16 . 0 . 62 . 4 . 83 .

70. 2 6. 1 12. 7 5. 9

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

251. 1 3. 9 -3. 1 395. 6 647. 5 OPTIO

N CAS E 4

390 . 12 . 402 .

16 . 0 . 62 . 4 . 83 .

70. 2 6. 1 12. 7 5. 9

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

251. 1 3. 9 -3. 1 395. 6 647. 5 OPTIO

N CAS E 5

390 . 12 . 402 .

16 . 0 . 62 . 4 . 83 .

70. 2 6. 1 12. 7 5. 9

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

251. 1 3. 9 -3. 1 395. 6 647. 5 OPTIO

N CAS E 6

390 . 12 . 402 .

16 . 0 . 62 . 4 . 83 .

70. 2 6. 1 12. 7 5. 9

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

251. 1 3. 9 -3. 1 395. 6 647. 5
ANNUALIZE

DCOST S V/. CHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X *TOTAL» 712 . 9 . 10 . 731 . 712 .

9 . 10 . 731 . 712 .

9 . 10 . 731 . 712 .

9 . 10 . 731 . 712 .

9 . 10 . 731 . 712 .

9 . 10 . 731 . 712 .

9 . 10 . 731 .TABLE 9 INDUSTRIA L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 75-10 0

FUELDEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L *TOTAL *
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGA S DISTILLATE FUE

LOI L RESIDUA LFUE LOI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L *TOTAL» TH E BAS E CAS E

166 . 9 . 175 .

11 . 0 . 39 . 4 . 54 .

43. 3 4. 3 6. 1 4. 2

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

138. 8 2. 8 -2. 2 255. 0 394. 4 OPTIO

N CAS E 1

166 . 9 . 175 .

11 . 0 . 39 . 4 . 54 .

43. 3 4. 3 8. 1 4. 2

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

138. 8 2. 8 -2. 2 255. 0 394. 4 OPTIO

N CAS E 2

166 . 9 . 175 .

11 . 0 . 39 . 4 . 54 .

43. 3 4. 3 8. 1 4. 2

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

138. 8 2. 8 -2. 2 255. 0 394. 4 OPTIO

N CASE 3

166 . 9 . 175 .

11 . 0 . 39 . 4 . 54 .

43. 3 4. 3 8. 1 4. 2

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

138. 8 2. 8 -2. 2 255. 0 394. 4 OPTIO

N CAS E 4

166 . 9 . 175 .

11 . 0 . 39 . 4 . 54 .

43. 3 4. 3 6. 1 4. 2

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

138. 8 2. 8 -2. 2 255. 0 394. 4 OPTIO

N CAS E 5

166 . 9 . 175 .

11 . 0 . 39 . 4 . 54 .

43. 3 4. 3 8. 1 4. 2

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

138. 8 2. 8 -2. 2 255. 0 394. 4 OPTIO

N CAS E 6

166 . 9 . 175 .

11 . 0 . 39 . 4 . 54 .

43. 3 4. 3 8. 1 4. 2

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

138. 8 2. 8 -2. 2 255. 0 394. 4
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0 0. 0
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X *TOTAL« 413 . 6 . 5 . 424 . 413 .

6 . 5 . 424 . 413 .ff5 . 424 . 413 .

6 . 5 . 424 . 413 .

6 .ui 424 . 413 .ffUl

424 . 413 .

6 . 5 . 424 .TABLE 1 0 INDUSTRIA LBOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 100-15 0

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA LGA S AN DOI L COA L »TOTAL«
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUELOI L RESIDUA LFUELOI L COA L *TOTAL«
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO # ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L *TOTAL» TH E BAS E CAS E

265 . 6 . 271 .

26 . 0 . 99 . 4 . 129 .

104. 8 8. 1 15. 2 8. 1

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

253. 6 6. 1 8. 0 631. 1 900. 9 OPTIO

N CAS E 1

267 . 4 . 271 .

26 . 0 . 100 . 3 . 129 .

69. 9 6. 0 16. 2 6. 0

-33. 3 -25. 9 6. 6 -25. 9

250. 2 6. 9 -0. 1 648. 7 905. 6 OPTIO

N CAS E 2

267 . 4 . 271 .

56 . 0 . 70 . 3 . 129 .

27. 9 3. 5 12. 5 3. 5

-73. 4 -56. 8 -17. 8 -56. 8

249. 8 9. 2 -1. 2 668. 4 926. 2 OPTIO

N CASE 3

270 . 1 . 271 .

58 . 0 . 70 . 1 . 129 .

26. 8 3. 5 12. 2 3. 5

-74. 4 -56. 8 -19. 7 -56. 8

244. 2 8. 3 -1. 4 675. 9 927. 0 OPTIO

N CAS E 4

271 . 0 . 271 .

72 . 0 . 57 . 0 . 129 .

14. 8 3. 4 12. 6 3. 4

-85. 9 -58. 0 -17. 1 -58. 0

242. 1 20. 1 -1. 6 681. 1 941. 8 OPTIO

N CAS E 5

271 . 0 . 271 .

72 . 0 . 57 . 0 . 129 .

12. 8 3. 4 12. 6 3. 4

-87. 8 -58. 0 -17. 1 -58. 0

242. 1 19. 8 -1. 6 681. 7 941. 9 OPTIO

N CAS E 6

271 . 0 . 271 .

85 . 0 . 44 . 0 . 129 .

3. 6 3. 2 12. 6 3. 2

-96. 6 -60. 5 -17. 1 -60. 5

241. 8 22. 0 -1. 9 682. 7 944. 7
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) *TOTAL« 0. 0 0. 5 2. 8 2. 9 4. 5 4. 6 4. 9
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X *TOTAL» 760 . 20 . 32 . 613 . 745 .

17 . 14 . 776 . 743 .

22 . 14 . 779 . 717 .

18 . 14 . 750 . 707 .

44 . 14 . 765 . 707 .

42 . 14 . 763 . 706 .

43 . 14 . 764 .TABLE 1 1 — INDUSTRIA

LBOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) 150-20 0

FUE LDEMAN D (NUMBE RO F UNITS ) NATURA LGA S AN

DOI L COA L •TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUE

LOI L RESIDUA LFUEL OI L COA L «TOTAL» EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L •TOTAL * TH E BAS E CAS E

134 . 1 . 135 .

24 . 0 . 86 . 1 . 111 .

81. 6 6. 5 13. 6 6. 5

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

160. 3 8. 0 4. 9 555. 2 728. 5 OPTIO

N CAS E 1

134 . 1 . 135 .

24 . 0 . 86 . 1 . 111 .

59. 7 5. 1 14. 6 5. 1

-26. 8 -21. 5 7. 4 -21. 5

160. 3 7. 5 -0. 2 565. 2 732. 8 OPTIO

N CAS E 2

134 . 1 . 135 .

50 . 0 . 60 . 1 . 111 .

23. 9 3. 1 12. 0 3. 1

-70. 7 -52. 3 -11. 8 -52. 3

160. 1 9. 2 -1. 1 581. 2 749. 3 OPTIO

N CASE 3

135 . 0 . 135 .

51 . 0 . 60 . 0 . 111 .

23. 4 3. 1 11. 8 3. 1

-71. 3 -52. 3 -13. 2 -52. 3

156. 7 8. 6 -1. 3 585. 1 749. 2 OPTIO

N CAS E 4

135 . 0 . 135 .

54 . 0 . 57 . 0 . 111 .

15. 7 3. 5 12. 9 3. 5

-80. 8 -46. 2 -5. 1 -46. 2

156. 7 21. 6 -0. 9 583. 3 760. 7 OPTIO

N CAS E 5

135 . 0 . 135 .

54 . 0 . 57 . 0 . 111 .

13. 4 3. 5 12. 9 3. 5

-83. 6 -46. 2 -5. 1 -46. 2

156. 7 22. 2 -0. 9 583. 3 761. 2 OPTIO

N CAS E 6

135 . 0 . 135 .

60 . 0 . 51 . 0 . 111 .

4. 1 3. 5 12. 9 3. 5

-95. 0 -46. 2 -5. 1 -46. 2

156. 6 23. 3 -1. 1 584. 1 763. 0
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 6 2. 9 2. 8 4. 4 4. 5 4. 7
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X •TOTAL * 471 . 20 . 20 . 512 . 471 .

20 . 10 . 502 . 470 .

21 . 10 . 501 . 456 .

19 . 10 . 486 . 456 .

47 . 10 . 514 . 456 .

48 . 10 . 514 . 456 .

45 . 10 . 512 .TABL E 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

FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GAS AN

OOI L COA L *TOTAL»
FUE LDEMAN D (10**1 2 BTUS ) NATURA L GAS DISTILLATE FUE

L OI L RESIDUA LFUE LOI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L *TOTAL» TH E BAS E CAS E

58 . 4 . 62 .

15 . 0 . 46 . 6 . 67 .

52. 1 3. 5 9. 4 3. 5

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

115. 3 6. 9 -1. 1 324. 2 445. 3 OPTIO

N CAS E 1

62 . 0 . 62 .

16 . 0 . 51 . 0 . 67 .

35. 3 3. 2 6. 9 3. 2

-32. 2 -8. 6 -5. 3 -8. 6

101. 4 4. 3 -5. 1 343. 0 443. 7 OPTIO

N CAS E 2

62 . 0 . 62 .

33 . 0 . 34 . 0 . 67 .

13. 7 2. 2 7. 8 2. 2

-73. 7 -37. 1 -17. 0 -37. 1

101. 4 8. 6 -6. 0 351. 5 455. 6 OPTIO

N CASE 3

62 . 0 . 62 .

33 . 0 . 34 . 0 . 67 .

13. 7 2. 2 7. 8 2. 2

-73. 7 -37. 1 -17. 0 -37. 1

101. 4 8. 6 -6. 0 351. 5 455. 6 OPTIO

N CAS E 4

62 . 0 . 62 .

34 . 0 . 33 . 0 . 67 .

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

-82. 0 -34. 3 -14. 9 -34. 3

101. 4 12. 3 -5. 6 351. 3 459. 5 OPTIO

N CAS E 5

62 . 0 . 62 .

34 . 0 . 33 . 0 . 67 .

7. 9 2. 3 8. 0 2. 3

-84. 8 -34. 3 -14. 9 -34. 3

101. 4 12. 7 -5. 6 351. 3 459. 8 OPTIO

N CAS E 6

62 . 0 . 62 .

35 . 0 . 32 . 0 . 67 .

2. 7 2. 2 8. 0 2. 2

-94. 8 -37. 1 -14. 9 -37. 1

101. 4 13. 6 -5. 7 351. 5 460. 8
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 -0. 4 2. 3 2. 3 3. 2 3. 3 3. 5
CAPITA L COST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X •TOTAL * 328 . 18 . 14 . 359 . 267 .

10 . 8 . 285 . 267 .

18 . 6 . 294 . 267 .

18 . 8 . 294 . 267 .

25 . 9 . 301 . 267 .

25 . 9 . 302 . 267 .

25 . 9 . 301 .TABLE 1 3 INDUSTRIA L BOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 25 0

FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL *
FUE LDEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUE

L OI L RESIDUA LFUE L OI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO I ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L •TOTAL * TH E BAS E CAS E

130 . 6 . 136 .

87 . 0 . 92 . 13 . 191 .

40. 9 4. 3 20. 8 4. 3

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

306. 1 8. 4 -19. 9 980. 0 1274. 6 OPTIO

N CAS E 1

130 . 6 . 136 .

87 . 0 . 92 . 13 . 191 .

40. 4 4. 3 20. 6 4. 3

-1. 2 0. 0 0. 0 0. 0

306. 1 8. 5 -19. 9 980. 0 1274. 7 OPTIO

N CAS E 2

130 . 6 . 136 .

87 . 0 . 92 . 13 . 191 .

40. 4 4. 3 20. 8 4. 3

-1. 2 0. 0 0. 0 0. 0

306. 1 8. 5 -19. 9 980. 0 1274. 7 OPTIO

N CASE 3

132 . 4 . 136 .

91 . 0 . 92 . 9 . 191 .

37. 9 4. 2 20. 0 4. 2

-7. 3 -2. 3 -3. 8 -2. 3

297. 2 8. 0 -20. 7 991. 4 1275. 9 OPTIO

N CAS E 4

129 . 7 . 136 .

107 . 0 . 70 . 15 . 191 .

16. 9 3. 4 20. 9 3. 4

-58. 7 -20. 9 0. 5 -20. 9

310. 2 27. 6 -20. 4 989. 7 1307. 2 OPTIO

N CAS E 5

124 . 12 . 136 .

107 . 0 . 59 . 26 . 191 .

13. 0 3. 1 22. 9 3. 1

-68. 2 -27. 9 10. 1 -27. 9

332. 1 38. 8 -18. 6 958. 6 1310. 9 OPTIO

N CAS E 6

124 . 12 . 136 .

113 . 0 . 52 . 26 . 191 .

5. 9 3. 0 23. 1 3. 0

-85. 6 -30. 2 11. 1 -30. 2

332. 1 41. 2 -18. 8 958. 8 1313. 2
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) *TOTAL * 0. 0 0. 0 0. 0 0. 1 2. 6 2. 9 3. 0
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X •TOTAL * 863 . 23 . 19 . 905 . 863 .

23 . 19 . 905 . 863 .

23 . 19 . 905 . 823 .

20 . 19 . 862 . 879 .

64 . 19 . 962 . 973 .

81 . 19 . 1074 . 973 .

85 . 19 . 1077 .TABL E 1 4 —

BOILE RSIZ E (MMBTU/HR ) > 10 0

FUE L DEMAND (NUMBERO F UNITS ) NATURAL GA S ANOOI L COAL *TOTAL *

FUE L DEMAND (10**1 2 BTUS ) NATURAL GA S DISTILLAT E FUE LOI L RESIOUAL FUE L OI L COA L *TOTAL *
EMISSION S (10** 3 TONS ) S0 2 P M NO X PMI O

EMISSION S VACHANG E FROM

BAS E CASE ) S0 2 P M NO X PMI O

ANNUALIZE DCOST S (10**6 , $1982 ) BOILE R FGDANDPM NO X FUE L *TOTAL «
ANNUALIZE DCOST S VACHANG E FRO HBAS E CASE ) •TOTAL *

CAPITAL COST S (10**6 , $1982 ) BOILE R FGDANDPM NO X *TOTAL » INDUSTRIALBOILE RNSP S NATIONALIMPACT S B YBOILERSIZE ,

TH E BAS E CAS E

587 . 17 . 604 .

152 . 0 . 323 . 23 . 498 .

279. 4 22. 4 59. 0 22. 4

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

835. 3 31. 5 -8. 1 2490. 5 3349. 2

0. 0

2422 . 82 . 84 . 2588 . OPTION

CAS E 1

593 . 11 . 604 .

153 . 0 . 329 . 17 . 498 .

205. 3 18. 6 60. 5 16. 6

-26. 5

- -17. 0 2. 5 -17. 0

818. 1 27. 1 -25. 2 2536. 9 3356. 8

0. 2

2347 . 70 . 51 . 2468 . OPTION

CAS E 2

593 . 11 . 604 .

225 . 0 . 257 . 17 . 498 .

105. 9 13. 1 53. 1 13. 1

-62. 1 -41. 5 -10. 0 -41. 5

817. 5 35. 5 -28. 2 2581. 1 3405. 8

1. 7

2343 . 84 . 51 . 2479 . OPTION

CAS E 3

599 . 5 . 604 .

232 . 0 . 257 . 9 . 498 .

101. 8 13. 0 51. 8 13. 0

-63. 6 -42. 0 -12. 2 -42. 0

799. 6 33. 6 -29. 3 2603. 9 3407. 7

1. 7

2264 . 76 . 51 . 2391 . 1986-199 0

OPTIO N CAS E 4

597 . 7 . 604 .

267 . 0 . 216 . 15 . 498 .

56 . B 12. 6 54. 4 12. 6

-79. 7 -43. 7 -7. 8 -43. 7

810. 4 81. 7 -28. 5 2605. 5 3469. 1

3. 6

2309 . 181 . 52 . 2542 . OPTION

CAS E 5

592 . 12 . 604 .

267 . 0 . 206 . 26 . 498 .

47. 1 12. 3 56. 4 12. 3

-83. 1 -45. 1 -4. 4 -45. 1

832. 3 93. 5 -26. 8 2574. 9 3473. 9

3. 7

2404 . 196 . 52 . 2652 . *

OPTIO N CAS E 6

592 . 12 . 604 .

294 . 0 . 178 . ; 26 . 498 . ; . i
i 16. 3 11. 9 56. 6 11. 9

-94. 2 -46. 9 j -4. 1 i . -46. 9 1 i ; i 832. 0 \ 100. 0 [ -27. 4 ! 2577. 1 3481. 7

4. 0

-

2402 . 199 . 52 . 2653 .TABLE 1 5 ~

BOILE RSIZ E (MMBTU/HR ) 100-25 0

FUE L DEMAN D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L •TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUEL OI L RESIOUA L FUE LOI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO
ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L •TOTAL *
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) •TOTAL *
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X •TOTAL * INDUSTRIA LBOILE RNSP S NATIONA

LIMPACT S B

YBOILE RSIZE ,

TH E BAS E CAS E

457 . 11 . 468 .

65 . 0 . 231 . 11 . 307 .

238. 5 16. 1 38. 2 18. 1

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

529. 2 23. 1 11. 8 1510. 5 2074. 7

0. 0

1559 . 59 . 66 . 1684 . OPTIO

N CAS E 1

463 . 5 . 468 .

66 . 0 . 237 . 4 . 307 .

164. 9 14. 3 39. 7 14. 3

-30. 9 -21. 0 3. 9 -21. 0

511. 9 16. 6 -5. 3 1556. 9 2082. 1

0. 4

1484 . 47 . 32 . 1563 . OPTIO

N CAS E 2

463 . 5 . 468 .

138 . 0 . 165 . 4 . 307 .

65. 5 8. 8 32. 3 6. 8

-72. 5 -51. 4 -15. 4 -51. 4

511. 3 27. 0 -8. 3 1601. 1 2131. 1

2. 7

1480 . 61 . 32 . 1574 . OPTIO

N CAS E 3

467 . 1 . 468 .

141 . 0 . 165 . 1 . 307 .

63. 9 8. 8 31. 8 8. 8

-73. 2 -51. 4 -16. 8 -51. 4

502. 4 25. 6 -8. 6 1612. 5 2131. 8

2. 8

1441 . 56 . 32 . 1529 . 1986-199 0

OPTIO N CAS E 4

468 . 0 . 468 .

160 . 0 . 147 . 0 . 307 .

39. 9 9. 2 33. 5 9. 2

-83. 3 -49. 2 -12. 3 -49. 2

500. 2 54. 1 -8. 1 1615. 8 2162. 0

4. 2

1431 . 116 . 33 . 1580 . OPTIO

N CAS E 5

468 . 0 . 468 .

160 . 0 . 147 . 0 . 307 .

34. 1 9. 2 33. 5 9. 2

-85. 7 -49. 2 -12. 3 -49. 2

500. 2 54. 7 -8. 2 1616. 3 2163. 0

4. 3

1431 . 115 . 33 . 1579 . OPTIO

N CAS E 6

468 . 0 . 468 .

181 . 0 . 126 . 0 . 307 .

10. 4 8. 9 33. 5 8. 9

-95. 6 -50. 8 -12. 3 -50. 8

499. 9 58. 9 -8. 6 1618. 3 2168. 5

4. 5

1429 . 114 . 33 . 1576 . 

### '

,

j

i

1 

## i i 

# i

i

### ; 

## i

l
j_ 

### *TABL E 1 6 — INDUSTRIA

L BOILE RNSP S NATIONA L IMPACT S BYBOILE RSIZE , 1986-199 0

BOILE RSIZ E (MMBTU/HR ) > 5 0

FUE L DEMAN

D (NUMBEROF UNITS ) NATURA L 6A S AN

D OI L COAL *TOTAL *
FUE L 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 *
EMISSIONS (10** 3 TONS ) S0 2 PM NOX PMI O
EMISSIONS VA CHANGE FRO

MBAS E CASE ) S0 2 PM NOX PMI O
ANNUALIZE D COST S (10**6 , $1982 ) BOILE R FG D AN DPM NOX FUE L *T0TAL * HE BAS E CAS E

1143

. 38

. 1181

.

178

. 0

. 425

. 32

. 634

.

392. 9 32. 8 79. 8 32. 5

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

1225. 2 38. 2 -13. 3 3141. 1 4391. 1 OPTIO

N CAS E 1

1149

. 32

. 1181

.

179

. 0

. 430

. 25

. 634

.

318. 6 29. 0 81. 3 28. 7

-16. 9 -11. 6 1. 9 -11. 7

1207. 9 33. 8 -30. 5 3187. 4 4398. 7 OPTIO

N CAS E 2

1149

. 32

. 1161

.

251

. 0

. 358

. 25

. 634

.

219. 4 23. 5 73. 9 23. 2

-44. 2 -28. 4 -7. 4 -28. 6

1207. 3 42. 2 -33. 5 3231. 6 4447. 7 OPTIO

N CAS E 3

1155

. 26

. 1181

.

258

. 0

. 358

. 17

. 634

.

215. 3 23. 4 72. 6 23. 1

-45. 2 -28. 7 -9. 0 -28. 9

1169. 4 40. 3 -34. 6 3254. 4 4449. 6 OPTIO

N CAS E 4

1153

. 28

. 1181

.

293

. 0

. 318

. 23

. 634

.

170. 3 23. 0 75. 2 22. 7

-56. 7 -29. 9 -5. 8 -30. 2

1200. 2 88. 4 -33. 7 3256. 1 4511. 0 OPTIO

N CAS E 5

1148

. 33

. 1161

.

293

. 0

. 307

. 34

. 634

.

160. 6 22. 7 77. 2 22. 4

-59. 1 -30. 8 -3. 3 -31. 1

1222. 1 100. 2 -32. 0 3225. 5 4515. 8 OPTION

CAS E 6

1148

. 33

. 1181

.

321

. 0

. 280

. 34

. 634

.

129. 8 22. 3 77. 4 22. 0

-67. 0 -32. 0 -3. 0 -32. 3

1221. 9 106. 7 -32. 7 3227. 6 4523. 5
ANNUALIZE D COST S VA CHANGE FRO

MBAS E CASE ) •TOTAL * 0. 0 0. 2 1. 3 1. 3 2. 7 2. 8 3. 0
CAPITA L COST S (10**6 , $1982 ) BOILE R FG D AN D PM NOX •TOTAL * 3547

. 97

. 99

. 3743

. 3472

.

85

. 65

. 3622

. 3468

.

99

. 65

. 3633

. 3389

.

91

. 65

. 3545

. 3434

.

196

. 66

. 3696

. 3529

.

212

. 67

. 3807

. 3527

.

214

. 67

. 3807

.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

FUE LDEMAN D (NUMBE RO F UNITS ) NATURA LGAS AN

DOI L COA L •TOTAL *
FUE L DEMAN D (10**1 2 BTUS ) NATURA LGAS DISTILLATE FUE

L OI L RESIDUA L FUE LOI L COA L •TOTAL *
EMISSIONS (10** 3 TONS ) S0 2 P M NO X PMIO
EMISSIONS VACHANG

E FRO M BAS E CASE ) S0 2 P M NO X PMIO ) ANNUALIZE

DCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X FUE L •TOTAL * TH E BAS E CAS E

2541 . 52 . 2593 .

212 . 0 . 518 . 35 . 766 .

500. 1 42. 4 98. 6 41. 4

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

1796. 4 40. 0 -15. 7 3785. 8 5606. 6 OPTIO

N CAS E 1

2547 . 46 . 2593 .

213 . 0 . 524 . 28 . 766 .

426. 0 38. 6 100. 0 37. 7

-14. 8 -9. 0 1. 4 -8. 9

1779. 1 35. 7 -32. 8 3832. 1 5614. 1 OPTIO

N CAS E 2

2547 . 46 . 2593 .

286 . 0 . 452 . 28 . 766 .

326. 6 33. 0 92. 7 32. 1

-34. 7 -22. 2 -6. 0 -22. 5

1778. 6 44. 1 -35. 8 3876. 3 5663. 2 OPTIO

N CASE 3

2553 . 40 . 2593 .

293 . 0 . 452 . 21 . 766 .

322. 4 33. 0 91. 3 32. 0

-35. 5 -22. 2 -7. 4 -22. 7

1760. 7 42. 2 -36. 9 3899. 1 5665. 0 OPTIO

N CAS E 4

2551 . 42 . 2593 .

328 . 0 . 411 . 27 . 766 .

277. 6 32. 6 94. 1 31. 7

-44. 5 -23. 1 -4. 6 -23. 4

1771. 4 90. 3 -36. 1 3900. 7 5726. 4 OPTIO

N CAS E 5

2546 . 47 . 2593 .

328 . 0 . 401 . 37 . 766 .

267. 9 32. 3 96. 0 31. 3

-46. 4 -23. 8 -2. 6 -24. 4

1793. 4 102. 1 -34. 4 3870. 1 5731. 2 OPTIO

N CAS E 6

2546 . 47 . 2593 .

355 . 0 . 374 . 37 . 766 .

237. 1 31. 9 96. 1 31. 0

-52. 6 -24. 8 -2. 5 -25. 1

1793. 1 108. 6 -35. 0 3872. 3 5739. 0
ANNUALIZE

DCOST S VACHANG

E FRO M BAS E CASE ) •TOTAL * 0. 0 0. 1 1. 0 1. 0 2. 1 2. 2 2. 4
CAPITA LCOST S (10**6 , $1982 ) BOILE R FG DAN DP M NO X •TOTAL * 4803 . 101 . 130 . 5033 . 4727 .

89 . 96 . 4912 . 4724 .

103 . 96 . 4923 . 4645 .

94 . 96 . 4835 . 4690 .

199 . 97 . 4987 . 4784 .

215 . 97 . 5097 . 4782 .

218 . 97 . 5097 .SIZE CLASS : 100-15 0 TABLE 1 8 — INDUSTRIA

LBOILE RNSP S REGIONA

LIMPACT S B

YBOILE RSIZE , 1986-199 0
S0 2 EMISSIONS (SHOR T TONS )

BAS E CAS E NE UENG . NAT . GAS 0. 0 RESI DOI L1001. 0 COA L0. 0 TOTA L1001. 0

OPTIO N CAS E 1 NE UENG . NAT . GAS 0. 0 RESIDOI L1001. 0 COA L0. 0 TOTA L1001. 0

OPTIO N CAS E 2 NE UENG . NAT . GAS 0. 0 RESI DOI L876. 0 COA L0. 0 TOTA L876. 0

OPTIO N CAS E 3 NE UENG . NAT . 6AS 0. 0 RESI DOI L876. 0 COA L0. 0 TOTA L876. 0

OPTIO N CAS E 4 NE M ENG . NAT . GAS 0. 0 RESIDOI L394. 0 COA L0. 0 TOTA L395. 0

OPTIO N CAS E 5 NE UENG . NAT . GAS 0. 0 RESI DOI L289. 0 COA L0. 0 TOTA L290. 0

OPTIO N CAS E 6 NE UENG . NAT . GAS 1. 0 RESIDOI L70. 0 COA L0. 0 TOTA L71. 0 N

N

N

N

N .Y./N.J . 0. 0 1659. 0 0. 0 1659. 0

.Y./N.J . 0. 0 1290. 0 0. 0 1290. 0

.Y./N.J . 0. 0 941. 0 0. 0 941. 0

.Y./N.J . 0. 0 941. 0 0. 0 941. 0

.Y./N.J . 0. 0 624. 0 0. 0 624. 0

N.Y./N.J .

N 0. 0 450. 0 0. 0 450. 0

.Y./N.J . 1. 0 84. 0 0. 0 85. 0 MID . ATL .

0. 0 7144. 0 0. 0 7144. 0

MID . ATL . 0. 0 6159. 0 0. 0 6159. 0

MID . ATL . 0. 0 3513. 0 0. 0 3513. 0

MID . ATL . 0. 0 3513. 0 0. 0 3513. 0

MID . ATL . 1. 0 2332. 0 0. 0 2333. 0

MID . ATL . 1. 0 1994. 0 0. 0 1995. 0

MID . ATL . 1. 0 665. 0 0. 0 665. 0 SO . ATL .

0. 0 15916. 0 3943. 0 19859. 0

SO . ATL . 0. 0 12524. 0 0. 0 12524. 0

SO . ATL . 0. 0 7157. 0 0. 0 7157. 0

SO . ATL . 0. 0 7157. 0 0. 0 7157. 0

SO . ATL . 0. 0 4162. 0 0. 0 4162. 0

SO . ATL . 0. 0 3598. 0 0. 0 3598. 0

SO . ATL . 2. 0 882. 0 0. 0 883. 0 MIDUES T

0. 0 19185. 0 0. 0 19185. 0

MIDUES T 0. 0 14835. 0 0. 0 14835. 0

MIDUES T 0. 0 8867. 0 0. 0 8867. 0

MIDUES T 0. 0 8867. 0 0. 0 8867. 0

MIDUES T 3. 0 3926. 0 0. 0 3929. 0

MIDUES T 3. 0 3356. 0 0. 0 3359. 0

MIDUES T 3. 0 1119. 0 0. 0 1122. 0 SO . UES T

4. 0 37679. 0 0. 0 37683. 0

SO . UES T 4. 0 20597. 0 0. 0 20601. 0

SO . UES T H. O 0. 0 0. 0 H. O

SO . UES T 11. 0 0. 0 0. 0 11. 0

SO . UES T 11. 0 0. 0 0. 0 11. 0

SO . UES T 11. 0 0. 0 0. 0 11. 0

SO . UES T 11. 0 0. 0 0. 0 11. 0 CENTRA

L 0. 0 9108. 0 0. 0 9108. 0

CENTRA L 0. 0 5290. 0 0. 0 5290. 0

CENTRA L 2. 0 O. O 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0 NO . CNTR

L 2. 0 0. 0 2712. 0 2714. 0

NO . CNTR

L 2. 0 0. 0 1964. 0 1966. 0

NO . CNTR

L 2. 0 0. 0 1352. 0 1354. 0

NO . CNTR

L 3. 0 0. 0 234. 0 237. 0

NO . CNTR

L 3. 0 0. 0 0. 0 3. 0

NO . CNTR

L 3. 0 0. 0 0. 0 3. 0

NO . CNTR

L 3. 0 0. 0 0. 0 3. 0 UES T

1. 0 3141. 0 0. 0 3142. 0

UES T 1. 0 2936. 0 0. 0 2937. 0

HES T 1. 0 2113. 0 0. 0 2114. 0

UES T 1. 0 2113. 0 0. 0 2114. 0

WES T 1. 0 1450. 0 0. 0 1452. 0

HES T 1. 0 1407. 0 0. 0 1409. 0

HES T 2. 0 344. 0 0. 0 346. 0 NO . UES T

0. 0 3267. 0 0. 0 3267. 0

NO . UES T 

### 6. 0 3267. 0 0. 0 3267. 0

NO . UES T 0. 0 3043. 0 0. 0 3043. 0

NO . UES T 0. 0 3043. 0 0. 0 3043. 0

NO . UES T 0. 0 1875. 0 0. 0 1875. 0

NO . UES T 0. 0 1665. 0 0. 0 1665. 0

NO . HES T 1. 0 432. 0 0. 0 432. 0 U S TOTA

L 8. 0 98101. 0 6655. 0 104764. 0

U S TOTA L 8. 0 67898. 0 1964. 0 69870. 0

U S TOTA L 17. 0 26509. 0 1352. 0 27878. 0

U S TOTA L 17. 0 26509. 0 234. 0 26760. 0

U S TOTA L 22. 0 14763. 0 0. 0 14785. 0

U S TOTA L 22. 0 12760. 0 0. 0 12782. 0

U S TOTA L 26. 0 3595. 0 0. 0 3621. 0SIZ E CLASS : 150-20 0 TABL E 1 9 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
S0 2 EMISSIONS (SHOR T TONS )

BAS E
NAT . GAS RESI DOI L COA L TOTA L CAS E

NE UENG . 0. 0 1141. 0 0. 0 1141. 0

OPTIO N CAS E 1
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 1141. 0 0. 0 1141. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 827. 0 0. 0 627. 0

OPTIO N CAS E 3
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 827. 0 0. 0 827. 0

OPTIO N CAS E 4
NAT . GAS RESI DOI L COA L TOTA L NE

M ENG . 0. 0 524. 0 0. 0 524. 0

OPTIO N CAS E 5
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 464. 0 0. 0 464. 0

OPTIO N CAS E 6
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 

# "8: 8 118. 0 N

N

N

N

N

N

N .Y./N.J . 0. 0 1095. 0 0. 0 1095. 0

.Y./N.J . 0. 0 1095. 0 0. 0 1095. 0

Y./N.J . 0. 0 781. 0 0. 0 781. 0

.Y./N.J . 0. 0 781. 0 0. 0 781. 0

.Y./N.J . 0. 0 644. 0 0. 0 644. 0

.Y./N.J . 0. 0 492. 0 0. 0 492. 0

.Y./N.J . 0. 0 164. 0 

### 16° : 8 MID . ATL .

1. 0 5196. 0 0. 0 5196. 0

MID . ATL . 1. 0 5196. 0 0. 0 5196. 0

MID . ATL . 1. 0 3095. 0 0. 0 3096. 0

MID . ATL . 1. 0 3095. 0 0. 0 3096. 0

MID . ATL . 1. 0 2277. 0 0. 0 2277. 0

MID . ATL . 1. 0 1946. 0 0. 0 1947. 0

MID . ATL . 1. 0 649. 0 0. 0 649. 0 SO . ATL .

0. 0 15434. 0 0. 0 15434. 0

SO . ATL . 0. 0 11640. 0 0. 0 11640. 0

SO . ATL . 0. 0 5944. 0 0. 0 5944. 0

SO . ATL . 0. 0 5944. 0 0. 0 5944. 0

SO . ATL . 0. 0 3780. 0 0. 0 3780. 0

SO . ATL . 0. 0 3104. 0 0. 0 3104. 0

SO . ATL . 0. 0 1007. 0 0. 0 1007. 0 MIDHES T

0. 0 14916. 0 0. 0 14916. 0

MIDUES T 0. 0 11959. 0 0. 0 11959. 0

MIOUES T 0. 0 6850. 0 0. 0 6850. 0

MIDUES T 0. 0 6850. 0 0. 0 6850. 0

MIDUES T 1. 0 4208. 0 0. 0 4209. 0

MIDUES T 1. 0 3598. 0 0. 0 3599. 0

MIDHES T 1. 0 1199. 0 0. 0 1200. 0 SO . HES T

5. 0 29967. 0 0. 0 - 29972. 0

SO . HES T 5. 0 16515. 0 0. 0 16520. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0

SO . HES T 11. 0 0. 0 0. 0 11. 0

SO . UES T 11. 0 0. 0 0. 0 11. 0 CENTRA

L 0. 0 5360. 0 0. 0 5360. 0

CENTRA L O. O 4325. 0 0. 0 4325. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 

# 8: 8 NO . CNTR

L 1. 0 1180. 0 1196. 0 2376. 0

NO . CNTR

L 1. 0 1180. 0 793. 0 1974. 0

NO . CNTR

L 1. 0 0. 0 546. 0 548. 0

NO . CNTR

L 2. 0 0. 0 0. 0 2. 0

NO . CNTR

L 2. 0 0. 0 0. 0 2. 0

NO . CNTR

L 2. 0 0. 0 0. 0 2. 0

NO . CNTR

L 2. 0 0. 0 0. 0 2. 0 HES T

0. 0 2316. 0 0. 0 2317. 0

HES T 0. 0 2035. 0 0. 0 2035. 0

HES T 0. 0 2035. 0 0. 0 2035. 0

UES T 0. 0 2035. 0 0. 0 2035. 0

HES T 0. 0 1656. 0 0. 0 1656. 0

UES T 0. 0 1556. 0 0. 0 1556. 0

HES T 2. 0 221. 0 0. 0 224. 0 NO . HES T

0. 0 3803. 0 0. 0 3603. 0

NO . UES T 

## 6. 0 3803. 0 0. 0 3803. 0

NO . UES T 0. 0 3803. 0 0. 0 3803. 0

NO . UES T 0. 0 3803. 0 0. 0 3803. 0

NO . HES T 

## 0. 6 2644. 0 0. 0 2644. 0

NO . HES T 0. 0 2202. 0 0. 0 2202. 0

NO . UES T 0. 0 734. 0 0. 0 734. 0 U S TOTA

L 7. 0 80409. 0 1196. 0 81612. 0

U S TOTA L 7. 0 58889. 0 793. 0 59689. 0

U S TOTA L 15. 0 23335. 0 546. 0 23896. 0

U S TOTA L 15. 0 23335. 0 0. 0 23350. 0

U S TOTA L 16. 0 15732. 0 0. 0 15748. 0

U S TOTA L 16. 0 13362. 0 0. 0 13378. 0

U S TOTA L 18. 0 4092. 0 

### 411?: 8SIZ ECLASS : 200-25 0 TABL E2 0 — INDUSTRIALBOILERNSP S REGIONALIMPACT S BYBOILERSIZE , 1986-199 0

S0 2 EMISSION S (SHOR T TONS )

BAS ECAS E

NAT . GA S RESI DOI L COA L TOTA L NE UENG .

0. 0 177. 0 0. 0 177. 0

OPTIO N CAS E1

NAT . GA S RESI DOI L COA L TOTA L NE HENG .

0. 0 177. 0 0. 0 177. 0

OPTIO N CAS E2

NAT . GA S RESI DOI L COA L TOTA L NE UENG .

0. 0 177. 0 0. 0 177. 0

OPTIO N CAS E3

NAT . GA S RESI DOI L COA L TOTA L NE HENG .

0. 0 177. 0 0. 0 177. 0

OPTIO N CAS E4

NAT . GA S RESI DOI L COA L TOTA L jNE HENG .

0. 0 177. 0 0. 0 177. 0

OPTIO N CAS E5

NAT . GA S RESI DOI L COA L TOTA L NE UENG .

0. 0 106. 0 0. 0 106. 0

OPTIO N CAS E6

NAT . GA S RESI DOI L COA L TOTA L NE UENG . 0. 0 0. 0 

## o: 8 N

•

N

N

N

N

N

N Y./N.J . 0. 0 643. 0 0. 0 643. 0

Y./N.J . 0. 0 643. 0 0. 0 643. 0

Y./N.J . 0. 0 643. 0 0. 0 643. 0

Y./N.J . 0. 0 643. 0 0. 0 643. 0

.Y./N.J . 0. 0 532. 0 0. 0 532. 0

.Y./N.J . 0. 0 455. 0 0. 0 455. 0

.Y./N.J . 0. 0 152. 0 0. 0 152. 0 MID . ATL .

0. 0 3500. 0 0. 0 3500. 0

MIO . ATL . 0. 0 3500. 0 0. 0 3500. 0

MID . ATL . 0. 0 2464. 0 0. 0 2464. 0

MID . ATL . 0. 0 2464. 0 0. 0 2464. 0

MID . ATL . 1. 0 1419. 0 0. 0 1420. 0

MIO . ATL . 1. 0 1213. 0 0. 0 1214. 0

MIO . ATL . 1. 0 404. 0 40 5 .' 0 SO . ATL .

0. 0 7421. 0 0. 0 7421. 0

SO . ATL . 0. 0 6312. 0 0. 0 6312. 0

SO . ATL . 0. 0 3746. 0 0. 0 3746. 0

SO . ATL . 0. 0 3746. 0 0. 0 3746. 0

SO . ATL . 0. 0 2433. 0 0. 0 2433. 0

SO . ATL . 0. 0 1935. 0 0. 0 1935. 0

SO . ATL . 0. 0 645. 0 0. 0 645. 0 MIDHES T

0. 0 5273. 0 12284. 0 17557. 0

MIDHES T 0. 0 9065. 0 0. 0 9065. 0

MIDHES T 0. 0 4809. 0 0. 0 4809 . O u

MIDUES T 0. 0 4809. 0 0. 0 4609. 0

MIDHES T 0. 0 3430. 0 0. 0 3430. 0

MIDHES T 0. 0 2932. 0 0. 0 2932. 0

MIDHES T 0. 0 977. 0 

### 977: 8 SO . HES T

4. 0 17297. 0 0. 0 17301. 0

SO . UES T 4. 0 12049. 0 0. 0 12053. 0

SO .

SO .

SO .

SO .

SO . HES T 8. 0 0. 0 0. 0 8. 0 .

HES T 8. 0 0. 0 0. 0 8. 0

HES T 8. 0 0. 0 0. 0 8. 0

UES T 8. 0 0. 0 0. 0 8. 0

HES T 8. 0 0. 0 0. 0 8. 0 CENTRA L

0. 0 2498. 0 0. 0 2496. 0

CENTRA L 0. 0 1685. 0 0. 0 1685. 0

CENTRA L 1. 0 0. 0 0. 0 1. 0

CENTRA L 1. 0 0. 0 0. 0 1. 0

CENTRA L 1. 0 0. 0 0. 0 1. 0

CENTRA L 1. 0 0. 0 0. 0 1. 0

CENTRA L 1. 0 0. 0 

# 8: 8 NO . CNTR L

1. 0 0. 0 1127. 0 1128. 0

NO .

NO .

NO .

NO .

NO .

NO . CNTR L 1. 0 0. 0 0. 0 1. 0

CNTR L 1. 0 0. 0 0. 0 1. 0

CNTR L 1. 0 0. 0 0. 0 1. 0

CNTR L 1. 0 0. 0 0. 0 1. 0

CNTR L 1. 0 0. 0 0. 0 1. 0

CNTR L 1. 0 

# 8: 8 1. 0 HES T

0. 0 704. 0 0. 0 704. 0

HES T 0. 0 704. 0 0. 0 704. 0

HES T 0. 0 704. 0 0. 0 704. 0

UES T 0. 0 704. 0 0. 0 704. 0

HES T 0. 0 596. 0 0. 0 596. 0

HES T 0. 0 596. 0 0. 0 596. 0

HES T 0. 0 267. 0 0. 0 267. 0 NO . HES T

0. 0 1138. 0 0. 0 1138. 0

NO . UES T 0. 0 1138. 0 0. 0 1138. 0

NO . HES T 0. 0 1138. 0 0. 0 1138. 0

N O . HES T 0. 0 1136. 0 0. 0 1138. 0

NO . HES T 0. 0 798. 0 0. 0 798. 0

NO . HES T 0. 0 683. 0 0. 0 683. 0

N O . HES T 0. 0 228. 0 0. 0 228. 0 U S TOTA L

5. 0 38650. 0 13412. 0 52066. 0

U S TOTA L 5. 0 35272. 0 0. 0 35277. 0

U S TOTA L 10. 0 13681. 0 0. 0 13691. 0

U S TOTA L 10. 0 13681. 0 0. 0 13691. 0

U S TOTA L 10. 0 9386. 0 0. 0 9396. 0

U S TOTA L 10. 0 7921. 0 0. 0 7931. 0

U S TOTA L 11. 0 2673. 0 0. 0 2683. 0SIZ E CLASS : > 25 0 TABL E 2 1 « INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0 S0 2 EMISSIONS (SHOR T TONS )

BAS E
NAT . GAS RESI DOI L COA L TOTA L CAS E

NE UENG . 0. 0 796. 0 0. 0 796. 0

OPTIO N CAS E 1
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 796. 0 0. 0 796. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 796. 0 0. 0 796. 0

OPTIO N CAS E 3
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 796. 0 0. 0 796. 0

OPTIO N CAS E 4
NAT . GAS RESI DOI L COA L TOTA L NEUENG .

0. 0 256. 0 0. 0 256. 0

OPTIO N CAS E 5
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 154. 0 0. 0 154. 0

OPTIO N CAS E 6
NAT . GA S RESI DOI L COA L TOTA L NE

UENG . 0. 0 51. 0 

### 5 

# ?: 8 N

•

N

N

N

N

N

N .Y./N.J . 0. 0 1734. 0 0. 0 1734. 0

Y./N.J . 0. 0 1734. 0 0. 0 1734. 0

.Y./N.J . 0. 0 1734. 0 0. 0 1734. 0

.Y./N.J . 0. 0 1734. 0 0. 0 1734. 0

.Y./N.J . 0. 0 796. 0 0. 0 797. 0

.Y./N.J . 0. 0 478. 0 0. 0 478. 0

.Y./N.J . 0. 0 159. 0 0. 0 160. 0 MID . ATL .

0. 0 5147. 0 0. 0 5147. 0

MID . ATL . 0. 0 5147. 0 0. 0 5147. 0

MID . ATL . 0. 0 5147. 0 0. 0 5147. 0

MID . ATL . 0. 0 5147. 0 0. 0 5147. 0

MID . ATL . 1. 0 1422. 0 1404. 0 2827. 0

MID . ATL . 1. 0 853. 0 1404. 0 2258. 0

MID . ATL . 1. 0 222. 0 971. 0 1195. 0 SO . ATL .

0. 0 10578. 0 0. 0 10578. 0

SO . ATL. . 0. 0 10578. 0 0. 0 10578. 0

SO . ATL . 0. 0 10578. 0 0. 0 10578. 0

SO . ATL . 0. 0 10578. 0 0. 0 10578. 0

SO . ATL . 0. 0 5147. 0 0. 0 5147. 0

SO . ATL . 0. 0 3316. 0 0. 0 3316. 0

SO . ATL . 0. 0 1058. 0 0. 0 1058. 0 MIDHES T

0. 0 12397. 0 0. 0 12397. 0

MIDHES T 0. 0 12397. 0 0. 0 12397. 0

MIDHES T 0. 0 12397. 0 0. 0 12397. 0

MIDUES T 0. 0 12397. 0 0. 0 12397. 0

MIOUES T 3. 0 3924. 0 0. 0 3927. 0

MIDUES T 3. 0 1075. 0 2341. 0 3419. 0

MIDHES T 4. 0 296. 0 2161. 0 2461. 0 S O

S O

SO

S O

S O

S O

S O HES T 20. 0 0. 0 0. 0 20. 0

HES T 20. 0 0. 0 0. 0 20. 0

. UES T 20. 0 0. 0 0. 0 20. 0 .

. UES T 20. 0 0. 0 0. 0 20. 0

. HES T 20. 0 0. 0 0. 0 20. 0

. HES T 20. 0 0. 0 0. 0 20. 0

. HES T 20. 0 0. 0 0. 0 20. 0 CENTRA

L 1. 0 0. 0 1893. 0 1694. 0

CENTRA L 1. 0 0. 0 1893. 0 1894. 0

CENTRA L 1. 0 0. 0 1893. 0 1894. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0

CENTRA L 2. 0 0. 0 0. 0 2. 0 NO . CNTR

L 2. 0 0. 0 2028. 0 2030. 0

NO . CNTR

L 2. 0 0. 0 2028. 0 2030. 0

NO . CNTR

L 2. 0 0. 0 2028. 0 2030. 0

NO . CNTR

L 2. 0 0. 0 1404. 0 1406. 0

NO . CNTR

L 2. 0 0. 0 936. 0 938. 0

NO . CNTR

L 2. 0 0. 0 936. 0 938. 0

NO . CNTR

L 2. 0 0. 0 325. 0 326. 0 HES T

3. 0 1137. 0 0. 0 1141. 0

HES T 3. 0 1137. 0 0. 0 1141. 0

UES T 3. 0 1137. 0 0. 0 1141. 0

HES T 3. 0 1137. 0 0. 0 1141. 0

HES T 3. 0 427. 0 0. 0 430. 0

UES T 3. 0 256. 0 0. 0 259. 0

UES T 3. 0 85. 0 0. 0 89. 0 NO . UES T

0. 0 3242. 0 1873. 0 5114. 0

NO . UES T 0. 0 3242. 0 1404. 0 4646. 0

NO . UES T 0. 0 3242. 0 1404. 0 4646. 0

NO . HES T 0. 0 3242. 0 1404. 0 4646. 0

NO . UES T 0. 0 1650. 0 936. 0 2586. 0

NO . HES T 0. 0 1218. 0 936. 0 2154. 0

NO . HES T 1. 0 216. 0 325. 0 542. 0 U S TOTA

L 26. 0 35031. 0 5794. 0 40852. 0

U S TOTA L 26. 0 35031. 0 5326. 0 40384. 0

U S TOTA L 26. 0 35031. 0 5326. 0 40384. 0

U S TOTA L 27. 0 35031. 0 2809. 0 37867. 0

U S TOTA L 32. 0 13621. 0 3277. 0 16931. 0

U S TOTA L 32. 0 7349. 0 5618. 0 12999. 0

U S TOTA L 34. 0 2087. 0 3782. 0 5903. 0SIZ E CLASS : 100-15 0 TABL E 2 2 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
FOSSI L FUEL DEMAN

D(10*»9BTUS )

BAS E CAS E NEHENG . NAT . GAS 548. 0 RESI DOI L2135. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E I NE UENG . NAT . GAS 548. 0 RESI DOI L2135. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E 2 NE UENG . NAT . GAS 548. 0 RESI DOI L2135. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E 3 NE UENG . NAT . GAS 548. 0 RESI DOI L2135. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E 4 NE UENG . NAT . GAS 1369. 0 RESI DOI L1314. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E 5 NE UENG . NAT . GAS 1369. 0 RESI DOI L1314. 0 COA L 0. 0 TOTA L 2683. 0

OPTIO N CAS E 6 NEHENG . NAT . GAS 1862. 0 RESIDOI L821. 0 COA L 0. 0 TOTA L 2683. 0 N

N

N

N

N

N

N .Y./N.J . 0. 0 3176. 0 0. 0 3176. 0

.Y./N.J . 0. 0 3176. 0 0. 0 3176. 0

.Y./N.J . 0. 0 3176. 0 0. 0 3176. 0

.Y./N.J . 0. 0 3176. 0 0. 0 3176. 0

.Y./N.J . 548. 0 2628. 0 0. 0 3176. 0

.Y./N.J . 548. 0 2628. 0 0. 0 3176. 0

.Y./N.J . 2190. 0 986. 0 0. 0 3176. 0 MID . ATL .

1095. 0 9143. 0 0. 0 10238. 0

MID . ATL . 1095. 0 9143. 0 0. 0 10238. 0

MID . ATL . 1095. 0 9143. 0 0. 0 10238. 0

MID . ATL . 1095. 0 9143. 0 0. 0 10238. 0

MID . ATL . 2464. 0 7775. 0 0. 0 10238. 0

MID . ATL . 2464. 0 7775. 0 0. 0 10238. 0

MID . ATL . 2464. 0 7775. 0 0. 0 10238. 0 SO . ATL .

0. 0 16261. 0 1424. 0 17684. 0

SO . ATL . 0. 0 17684. 0 0. 0 17684. 0

SO . ATL . 0. 0 17684. 0 0. 0 17684. 0

SO . ATL . 0. 0 17684. 0 0. 0 17684. 0

SO . ATL . 0. 0 17684. 0 0. 0 17684. 0

SO . ATL . 0. 0 17684. 0 0. 0 17684. 0

SO . ATL . 5475. 0 12209. 0 0. 0 17684. 0 MIDHES T

821. 0 22119. 0 0. 0 22940. 0

MIDUES T 621. 0 22119. 0 0. 0 22940. 0

MIDHES T 821. 0 22119. 0 0. 0 22940. 0

MIDHES T 821. 0 22119. 0 0. 0 22940. 0

MIDUES T 9855. 0 13085. 0 0. 0 22940. 0

MIDHES T 9855. 0 13085. 0 0. 0 22940. 0

MIDHES T 9855. 0 13085. 0 0. 0 22940. 0 SO . HES T

13523. 0 24090. 0 0. 0 37613. 0

SO . UES T 13523. 0 24090. 0 0. 0 37613. 0

SO . HES T 37613. 0 0. 0 0. 0 37613. 0

SO . HES T 37613. 0 0. 0 0. 0 37613. 0

SO . HES T 37613. 0 0. 0 0. 0 37613. 0

SO . UES T 37613. 0 0. 0 0. 0 37613. 0

SO . HES T 37613. 0 0. 0 0. 0 37613. 0 CENTRA

L 0. 0 6187. 0 0. 0 6187. 0

CENTRA L 0. 0 6187. 0 0. 0 6187. 0

CENTRA L 6187. 0 0. 0 0. 0 6107. 0

CENTRA L 6187. 0 0. 0 0. 0 6187. 0

CENTRA L 6187. 0 0. 0 0. 0 6187. 0

CENTRA L 6187. 0 0. 0 0. 0 6187. 0

CENTRA L 6187. 0 0. 0 0. 0 6187. 0 NO . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0

NO . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0

NO . CNTR

L 6515. 0 0. 0 2847. 0 9362. 0

NO . CNTR

L 8651. 0 0. 0 712. 0 9362. 0

NO . CNTR

L 9362. 0 0. 0 0. 0 9362. 0

NO . CNTR

L 9362. 0 0. 0 0. 0 9362. 0

NO . CNTR

L 9362. 0 0. 0 0. 0 9362. 0 HES T

3230. 0 7994. 0 0. 0 11224. 0

HES T 3230. 0 7994. 0 0. 0 11224. 0

HES T 3230. 0 7994. 0 0. 0 11224. 0

HES T 3230. 0 7994. 0 0. 0 11224. 0

HES T 4599. 0 6625. 0 0. 0 11224. 0

UES T 4599. 0 6625. 0 0. 0 11224. 0

UES T 7829. 0 3395. 0 0. 0 11224. 0 NO . UES T

0. 0 7501. 0 0. 0 7501. 0

NO . HES T 0. 0 7501. 0 0. 0 7501. 0

NO . UES T 0. 0 7501. 0 0. 0 7501. 0

NO . HES T 0. 0 7501. 0 0. 0 7501. 0

NO . HES T 0. 0 7501. 0 0. 0 7501. 0

NO . HES T 0. 0 7501. 0 0. 0 7501. 0

NO . UES T 2190. 0 5311. 0 7501: o U S TOTA

L 25733. 0 98605. 0 4271. 0 128608. 0

U S TOTA L 25733. 0 100028. 0 2847. 0 128608. 0

U S TOTA L 56009. 0 69752. 0 2847. 0 128608. 0

U S TOTA L 58145. 0 69752. 0 712. 0 128608. 0

U S TOTA L 71996. 0 56612. 0 0. 0 128608. 0

U S TOTA L 71996. 0 56612. 0 0. 0 128608. 0

U S TOTA L 85027. 0 43581. 0 128608: 0SIZ E CUSS : 150-20 0 TABLE 2 3 « INDUSTRIA L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
FOSSI L FUE

L DEMAN D(10** 9 BTUS )

BAS E CAS E NE UENG . NAT . GAS 0. 0 RESIDOI L2070. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 1 NE UENG . NAT . GAS 0. 0 RESI DOI L2070. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 2 NE UENG . NAT . GAS 0. 0 RESI DOI L2070. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 3 NE UENG . NAT . GAS 0. 0 RESI DOI L 2070. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 4 NE N ENG . NAT . GAS 0. 0 RESI DOI L 2070. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 5 NE HENG . NAT . GAS 0. 0 RESI DOI L2070. 0 COA L 0. 0 TOTA L 2070. 0

OPTIO N CAS E 6 NE UENG . NAT . GAS 690. 0 RESIDOI L 1380. 0 COA L 0. 0 TOTA L 2070. 0 N

N

N

N

N

N

N .Y./N.J . 1380. 0 2529. 0 0. 0 3909. 0

.Y./N.J . 1380. 0 2529. 0 0. 0 3909. 0

•Y./N.J . 1380. 0 2529. 0 0. 0 3909. 0

.Y./N.J . 1380. 0 2529. 0 0. 0 3909. 0

.Y./N.J . 1380. 0 2529. 0 0. 0 3909. 0

.Y./N.J . 1380. 0 2529. 0 0. 0 3909. 0

.Y./N.J . 1380. 0 2529. 0 0. 0 3909. 0 MID . ATL .

1840. 0 7972. 0 0. 0 9811. 0

MID . ATL . 1840. 0 7972. 0 0. 0 9811. 0

MID . ATL . 1640. 0 7972. 0 0. 0 9811. 0

MID . ATL . 1840. 0 7972. 0 0. 0 9811. 0

MID . ATL . 2223. 0 7588. 0 0. 0 9811. 0

MID . ATL . 2223. 0 7588. 0 0. 0 9811. 0

MID . ATL . 2223. 0 7588. 0 0. 0 9811. 0 SO . ATL .

0. 0 14717. 0 0. 0 14717. 0

SO . ATL . 0. 0 14717. 0 0. 0 14717. 0

SO . ATL . 0. 0 14717. 0 0. 0 14717. 0

SO . ATL . 0. 0 14717. 0 0. 0 14717. 0

SO . ATL . 0. 0 14717. 0 0. 0 14717. 0

SO . ATL . 0. 0 14717. 0 0. 0 14717. 0

SO . ATL . 0.0 . 14717. 0 0. 0 14717. 0 MIDUES T

0. 0 16786. 0 0. 0 16786. 0

MIDUES T 0. 0 16786. 0 0. 0 16786. 0

MIDHES T 0. 0
' 16786. 0 0. 0 16786. 0

MIDUES T 0. 0 16786. 0 0. 0 16786. 0

MIDUES T 2759. 0 14027. 0 0. 0 16786. 0

MIDUES T 2759. 0 14027. 0 0. 0 16766. 0

MIDHES T 2759. 0 14027. 0 0. 0 16786. 0 SO . HES T

15867. 0 19316. 0 0. 0 35182. 0

SO . HES T 15867. 0 19316. 0 0. 0 35182. 0

SO . HES T 35182. 0 0. 0 0. 0 35162. 0

SO . HES T 35182. 0 0. 0 0. 0 35182. 0

SO . HES T 35182. 0 0. 0 0. 0 35182. 0

SO . HES T 35182. 0 0. 0 0. 0 35182. 0

SO . HES T 35182. 0 0. 0 35182: 0 CENTRA

L 0. 0 5059. 0 0. 0 5059. 0

CENTRA L 0. 0 5059. 0 0. 0 5059. 0

CENTRA L 5059. 0 0. 0 0. 0 .5059. 0

CENTRA L 5059. 0 0. 0 0. 0 5059. 0

CENTRA L 5059. 0 0. 0 0. 0 5059. 0

CENTRA L 5059. 0 0. 0 O. O 5059. 0

CENTRA L 5059. 0 0. 0 0. 0 5059. 0 NO . CNTR

L 3449. 0 1380. 0 1150. 0 5979. 0

NO . CNTR

L 3449. 0 1380. 0 1150. 0 5979. 0

NO . CNTR

L 4829. 0 0. 0 1150. 0 5979. 0

NO . CNTR

L 5979. 0 0. 0 0. 0 5979. 0

NO . CNTR

L 5979. 0 0. 0 0. 0 5979. 0

NO . CNTR

L 5979. 0 0. 0 0. 0 5979. 0

NO . CNTR

L 5979. 0 0. 0 0. 0 5979. 0 HES T

1380. 0 7128. 0 0. 0 8508. 0

HES T 1380. 0 7128. 0 0. 0 8508. 0

UES T 1380. 0 7128. 0 0. 0 8508. 0

HES T 1380. 0 7128. 0 0. 0 8508. 0

HES T 1380. 0 7128. 0 0. 0 8508. 0

HES T 1380. 0 7128. 0 0. 0 8508. 0

UES T 7128. 0 1380. 0 0. 0 8508. 0 NO . UES T

0. 0 9198. 0 0. 0 9198. 0

NO . HES T 0. 0 9198. 0 0. 0 9198. 0

NO . UES T 0. 0 9198. 0 0. 0 9198. 0

NO . UES T 0. 0 9198. 0 0. 0 9198. 0

NO . UES T 0. 0 9198. 0 0. 0 9198. 0

NO . UES T 0. 0 9198. 0 0. 0 9198. 0

NO . HES T 0. 0 9198. 0 9198: 0 U S TOTA

L 23915. 0 86155. 0 1150. 0 111219. 0

U S TOTA L 23915. 0 86155. 0 1150. 0 111219. 0

U S TOTA L 49669. 0 60400. 0 1150. 0 111219. 0

U S TOTA L 50819. 0 60400. 0 0. 0 111219. 0

U S TOTA L 53962. 0 57258. 0 0. 0 111219. 0

U S TOTA L 53962. 0 57258. 0 0. 0 111219. 0

U S TOTA L 60400. 0 50819. 0 0. 0 111219. 0SIZ ECLASS : 200-25 0 TABL E2 4 — INDUSTRIALBOILERNSP S REGIONALIMPACT S BYBOILERSIZE , 1986-199 0

FOSSI LFUE LDEMAN

D(10** 9 BTUS )

BAS E
NAT . GAS RESIOOI L COA L TOTA L CAS E

NE UENG . 0. 0 887. 0 0. 0 887. 0

OPTIO N CAS E 1
NAT . GAS RESIDOI L COA L TOTA L NE

UENG . 0. 0 887. 0 0. 0 887. 0

OPTIO N CAS E 2
NAT . GAS RESIDOI L COA L TOTA L NE

UENG . 0. 0 887. 0 0. 0 887. 0

OPTIO N CAS E 3
NAT . GA S RESI DOI L COA L TOTA L NE

UENG . 0. 0 887. 0 0. 0 887. 0

OPTIO N CAS E 4
NAT . GAS RESI OOI L COA L TOTA L NEHENG .

0. 0 887. 0 0. 0 887. 0

OPTIO N CAS E 5
NAT . GA S RESI DOI L COA L TOTA L NEHENG .

0. 0 887. 0 0. 0 887. 0

OPTIO N CAS E 6
NAT . GAS RESIDOI L COA L TOTA L NE

UENG . 887. 0 0. 0 0. 0 887. 0 N

N

N

N

N

N

N .Y./N.J . 0. 0 1774. 0 0. 0 1774. 0

.Y./N.J . 0. 0 1774. 0 0. 0 1774. 0

.Y./N.J . 0. 0 1774. 0 0. 0 1774. 0

.Y./N.J . 0. 0 1774. 0 0. 0 1774. 0

.Y./N.J . 0. 0 1774. 0 0. 0 1774. 0

.Y./N.J . 0. 0 1774. 0 0. 0 1774. 0

.Y./N.J . 0. 0 1774. 0 0. 0 1774. 0 MID . ATL .

0. 0 6504. 0 0. 0 6504. 0

MID . ATL . 0. 0 6504. 0 0. 0 6504. 0

' MID . ATL . 0. 0 6504. 0 0. 0 6504. 0

MID . ATL . 0. 0 6504. 0 0. 0 6504. 0

MID . ATL . 1774. 0 4730. 0 0. 0 6504. 0

MID . ATL . 1774. 0 4730. 0 0. 0 6504. 0

MIO . ATL . 1774. 0 4730. 0 0. 0 6504. 0 SO . ATL .

0. 0 9067. 0 0. 0 9067. 0

SO . ATL . 0. 0 9067. 0 0. 0 9067. 0

SO . ATL . 0. 0 9067. 0 0. 0 9067. 0

SO . ATL . 0. 0 9067. 0 0. 0 9067. 0

SO . ATL . 0. 0 9067. 0 0. 0 9067. 0

SO . ATL . 0. 0 9067. 0 0. 0 9067. 0

SO . ATL . 0. 0 9067. 0 0. 0 9067. 0 MIDHES T

0. 0 6997. 0 4435. 0 11432. 0

MIDUES T 0. 0 11432. 0 0. 0 11432. 0

MIDUES T 0. 0 11432. 0 0. 0 11432. 0

MIDHES T 0. 0 11432. 0 0. 0 11432. 0

MIDHES T 0. 0 11432. 0 0. 0 11432. 0

MIDHES T 0. 0 11432. 0 0. 0 11432. 0

MIDHES T 0. 0 11432. 0 0. 0 11432. 0 SO . HES T

12319. 0 14093. 0 0. 0 26411. 0

SO . HES T 12319. 0 14093. 0 0. 0 26411. 0

SO . UES T 26411. 0 0. 0 0. 0 26411. 0

SO . HES T 26411. 0 0. 0 0. 0 26411. 0

SO . HES T 26411. 0 0. 0 0. 0 26411. 0

SO . UES T 26411. 0 0. 0 0. 0 26411. 0

SO . HES T 26411. 0 0. 0 0. 0 26411. 0 CENTRA

L 0. 0 1971. 0 0. 0 1971. 0

CENTRA L 0. 0 1971. 0 0. 0 1971. 0

CENTRA L 1971. 0 0. 0 0. 0 1971. 0

CENTRA L 1971. 0 0. 0 0. 0 1971. 0

CENTRA L 1971. 0 0. 0 0. 0 1971. 0

CENTRA L 1971. 0 0. 0 0. 0 1971. 0

CENTRA L 1971. 0 0. 0 0. 0 1971. 0 NO . CNTR

L 2168. 0 0. 0 1084. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0 HES T

887. 0 2168. 0 0. 0 3055. 0

HES T 887. 0 2168. 0 0. 0 3055. 0

HES T 887. 0 2168. 0 0. 0 3055. 0

HES T 887. 0 2168. 0 0. 0 3055. 0

HES T 887. 0 2168. 0 0. 0 3055. 0

UES T 887. 0 2168. 0 0. 0 3055. 0

HES T 887. 0 2168. 0 0. 0 3055. 0 NO . UES T

0. 0 2661. 0 0. 0 2661. 0

NO . UES T 0. 0 2661. 0 0. 0 2661. 0

NO . HES T 0. 0 2661. 0 0. 0 2661. 0

NO . UES T 0. 0 2661. 0 0. 0 2661. 0

NO . UES T 0. 0 2661. 0 0. 0 2661. 0

NO . HES T 0. 0 2661. 0 0. 0 2661. 0

NO . HES T 0. 0 2661. 0 2661: o U S TOTA

L 15374. 0 46121. 0 5519. 0 67014. 0

U S TOTA L 16458. 0 50556. 0 0. 0 67014. 0

U S TOTA L 32521. 0 34492. 0 0. 0 67014. 0

U S TOTA L 32521. 0 34492. 0 0. 0 67014. 0

U S TOTA L 34295. 0 32719. 0 0. 0 67014. 0

U S TOTA L 34295. 0 32719. 0 0. 0 67014. 0

U S TOTA L 35182. 0 

### SUB 

# 8 : 8 67014. 0SIZ E CUSS : > 25 0

BAS E CAS E NEHENG . NAT . GAS 0. 0 RESI DOI L1993. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 1 NE UENG . NAT . GAS 0. 0 RESI DOI L1993. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 2 NE UENG . NAT . GAS 0. 0 RESI DOI L 1993. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 3 NE UENG . NAT . GAS 0. 0 RESI DOI L1993. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 4 NE W ENG . NAT . GAS 712. 0 RESI DOI L 1281. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 5 NEHENG . NAT . GAS 712. 0 RESI DOI L 1281. 0 COA L 0. 0 TOTA L 1993. 0

OPTIO N CAS E 6 NE UENG . NAT . GAS 712. 0 RESI DOI L 1281. 0 COA L 0. 0 TOTA L 1993. 0 TABLE 2 5 — INDUSTRIA

L BOILE R

N.Y./N.J . 0. 0 5409. 0 0. 0 5409. 0

N.Y./N.J . 0. 0 5409. 0 0. 0 5409. 0

N.Y./N.J . 0. 0 5409. 0 0. 0 5409. 0

N.Y./N.J . 0. 0 5409. 0 0. 0 5409. 0

N.Y./N.J . 1424. 0 3986. 0 0. 0 5409. 0

N.Y./N.J . 1424. 0 3986. 0 0. 0 5409. 0

N.Y./N.J . 1424. 0 3986. 0 0. 0 5409. 0 MID . ATL .

1424. 0 15516. 0 0. 0 16940. 0

MID . ATL . 1424. 0 15516. 0 0. 0 16940. 0

MID . ATL . 1424. 0 15516. 0 0. 0 16940. 0

MID . ATL . 1424. 0 15516. 0 0. 0 16940. 0

MID . ATL . 3416. 0 7117. 0 6406. 0 16940. 0

MID . ATL . 3416. 0 7117. 0 6406. 0 16940. 0

MID . ATL . 4982. 0 5552. 0 6406. 0 16940. 0 FOSSI L

SO . ATL . 0. 0 26477. 0 0. 0 26477. 0

SO . ATL . 0. 0 26477. 0 0. 0 26477. 0

SO . ATL . 0. 0 26477. 0 0. 0 26477. 0

SO . ATL . 0. 0 26477. 0 0. 0 26477. 0

SO . ATL . 0. 0 26477. 0 0. 0 26477. 0

SO . ATL . 0. 0 26477. 0 0. 0 26477. 0

SO . ATL . 0. 0 26477. 0 0. 0 26477. 0 NSP S REGIONA L IMPACT S
FUE L DEMAN D

MIDUES T 0. 0 31032. 0 0. 0 31032. 0

MIDHES T 0. 0 31032. 0 0. 0 31032. 0

MIOUES T 0. 0 31032. 0 0. 0 31032. 0

MIOUES T 0. 0 31032. 0 0. 0 31032. 0

MIDUES T 11388. 0 19644. 0 0. 0 31032. 0

MIDHES T 11388. 0 8968. 0 10676. 0 31032. 0

MIDHES T 12954. 0 7402. 0 10676. 0 31032. 0 (10** 9

SO . HES T 65766. 0 0. 0 0. 6 65766. 0

SO . HES T 65766. 0 0. 0 0. 0 65766. 0

SO . UES T 65766. 0 0. 0 0. 0 65766. 0

SO . UES T 65766. 0 0. 0 0. 0 65766. 0

SO . HES T 65766. 0 0. 0 0. 0 65766. 0

SO . HES T 65766. 0 0. 0 0. 0 65766. 0

SO . HES T 65766. 0 0. 0 0. 0 65766. 0 B

YBOILE R
BTUS )

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0 6690. 0

CENTRA L 2705. 0 0. 0 3986. 0

. 6690. 0

CENTRA L 6690. 0 0. 0 0. 0 6690. 0

CENTRA L 6690. 0 0. 0 0. 0 6690. 0

CENTRA L 6690. 0 0. 0 0. 0 6690. 0

CENTRA L 6690. 0 0. 0 0. 0 6690. 0 SIZE , 1986 -

NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 5979. 0 0. 0 4271. 0 10249. 0

NO . CNTR

L 5979. 0 0. 0 4271. 0 102'i9. 0 199 0

UES T 10676. 0 2847. 0 0. 0 13523. 0

HES T 10676. 0 2847. 0 0. 0 13523. 0

HES T 10676. 0 2847. 0 0. 0 13523. 0

UES T 10676. 0 2847. 0 0. 0 13523. 0

HES T 11388. 0 2135. 0 0. 0 13523. 0

HES T 11388. 0 2135. 0 0. 0 13523. 0

HES T 11388. 0 2135. 0 0. 0 13523. 0 NO . HES T

0. 0 8968. 0 4271. 0 13239. 0

NO , HES T 0. 0 8968. 0 4271. 0 13239. 0

NO . UES T 0. 0 8968. 0 4271. 0 13239. 0

NO . UES T 0. 0 8968. 0 4271. 0 13239. 0

NO . HES T 0. 0 8968. 0 4271. 0 13239. 0

NO . HES T 0. 0 8968. 0 4271. 0 13239. 0

NO . HES T 3559. 0 5409. 0 4271. 0 13239. 0 U S TOTA

L 86549. 0 92243. 0 12527. 0 191318. 0

U S TOTA L 86549. 0 92243. 0 12527. 0 191318. 0

U S TOTA L 66549. 0 92243. 0 12527. 0 191318. 0

U S TOTA L 90535. 0 92243. 0 8541. 0 191318. 0

U S TOTA L 106762. 0 69609. 0 14947. 0 191318. 0

U S TOTA L 106762. 0 58933. 0 25623. 0 191316. 0

U S TOTA L 113453. 0 52242. 0 25623. 0 191318. 0 »

y

•



### -

-SIZ E CUSS : 100-15 0 TABL E 2 6 — INOUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10** 6 198 2 $ )

BAS E CAS E NEHENG . N.Y./N.J . NAT . GAS 4. 7 0. 0 RESI DOI L 15. 9 23. 1 COA L0. 0 0. 0 TOTA L20. 6 23. 1

OPTIO N CAS E 1 NEHENG . N.Y./N.J . NAT . GAS 4. 7 0. 0 RESI DOI L15. 9 23. 2 COA L0. 0 0. 0 TOTA L20. 6 23. 2

OPTIO N CAS E 2 NEHENG . N.Y./N.J . NAT . GAS 4. 7 0. 0 RESI DOI L16. 0 23. 5 COA L0. 0 0. 0 TOTA L20. 7 23. 5

OPTIO N CAS E 3 NE UENG . N.Y./N.J . NAT . GAS 4. 7 0. 0 RESI DOI L 16. 0 23. 5 COA L0. 0 0. 0 TOTA L20. 7 23. 5

OPTIO N CAS E 4 HE W ENG . N.Y./N.J . NAT . GAS 11. 7 4. 6 RESI DOI L9. 5 19. 3 COA L0. 0 0. 0 TOTA L21. 2 24. 0

OPTIO N CAS E 5 NEHENG . N.Y . NAT . GAS 11. 7 RESI DOI L9. 5 COA L0. 0 TOTA L21. 1

OPTIO N CAS E 6 NEHENG . N.Y . NAT . GAS 15. 3 RESI OOI L 5. 8 COA L0. 0 TOTA L21. 1 /N.J . 4. 6 19. 4 0. 0 24. 0

/N.J . 16. 3 7. 4 0. 0 23. 7 MID . ATL .

9. 2 63. 5 0. 0 72. 8

MID . ATL . 9. 2 63. 6 0. 0 72. 9

MID .

MI D ATL . 9. 2 65. 9 0. 0 75. 1

ATL . 9. 2 65. 9 0. 0 75. 1

MID . ATL . 20. 8 55. 9 0. 0 76. 7

MID . ATL . 20. 8 56. 0 0. 0 76. 8

MID . ATL . 20. 8 56. 3 

# 7?: ? SO . ATL .

0. 0 114. 9 10. 0 124. 9

SO . ATL . 0. 0 125. 1 0. 0 125. 1

SO . ATL . 0. 0 129. 8 0. 0 129. 8

SO . ATL . 0. 0 129. 8 0. 0 129. 8

SO . ATL . 0. 0 135. 5 0. 0 135. 5

SO ATL . 0. 0 135. 4 0. 0 135. 4

SO . ATL . 47. 7 89. 3 0. 0 137. 0 MIDHES T

7. 0 160. 0 0. 0 167. 0

MIDHES T 7. 0 160. 4 0. 0 167. 4

MIDHES T 7. 0 165. 8 0. 0 172. 8

MIDHES T 7. 0 165. 8 0. 0 172. 8

MIDUES T 80. 7 96. 3 0. 0 177. 1

MIDUES T 80. 7 96. 5 0. 0 177. 2

MIDUES T 80. 7 97. 0 0. 0 177. 7 SO . HES T

93. 6 157. 9 0. 6 251. 5

SO . HES T 93. 6 161. 0 0. 0 254. 6

SO . UES T 260. 5 0. 0 0. 0 260. 5

SO . HES T 260. 5 0. 0 0. 0 260. 5

SO . HES T 260. 5 0. 0 0. 0 260. 5

SO . HES T 260. 5 0. 0 0. 0 260. 5

SO . HES T 260. 5 0. 0 0. 0 260. 5 CENTRA

L 0. 0 44. 2 0. 0 44. 2

CENTRA L 0. 0 44. 7 0. 0 44. 7

CENTRA L 45. 6 0. 0 0. 0 45. 6

CENTRA L 45. 6 0. 0 0. 0 45. 6

CENTRA L 45. 6 0. 0 0. 0 45. 6 NO . CNTR

L 46. 5 0. 0 17. 0 63. 4

NO .

NO .

NO .

NO . CNTR

L 46. 5 0. 0 17. 2 63. 7

CNTR L 46. 5 0. 0 17. 2 63. 7

CNTR L 59. 7 0. 0 4. 8 64. 5

CNTR L 64. 2 0. 0 0. 0 64. 2 HES T

25. 8 55. 5 0. 0 81. 3

UES T 25. 8 55. 5 0. 0 81. 3

HES T 25. 8 56. 2 0. 0 82. 0

HES T 25. 8 56. 2 0. 0 82. 0

HES T 36. 9 45. 8 0. 0 82. 7 NO .

NO .

NO .

NO .

NO . HES T 0. 0 52. 1 0. 0 52. 1

UES T 0. 0 52. 1 0. 0 52. 1

HES T 0. 0 52. 3 0. 0 52. 3

UES T 0. 0 52. 3 0. 0 52. 3

UES T 0. 0 54. 3 0. 0 54. 3 U S TOTA

L 186. 7 687. 2 27. 0 900. 9

U S TOTA L 186. 7 701. 7 17. 2 905. 6

U S TOTA L 399. 3 509. 6 17. 2 926. 2

U S TOTA L 412. 6 509. 6 4. 8 927. 0

U S TOTA L 525. 1 416. 7 0. 0 941. 8

CENTRA L 45. 6 0. 0 0. 0 45. 6

CENTRA L 45. 6 0. 0 0. 0 45. 6 NO .

NO . CNTR

L 64. 2 0. 0 0. 0 64. 2

CNTR L 64. 2 0. 0 0. 0 64. 2 HES T

36. 9 45. 8 0. 0 82. 7

HES T 59. 0
82. 7 NO . HES T

0. 0 54. 3 0. 0 54. 3

NO . HES T 18. 1 36. 8 0. 0 54. 9 U S TOTA

L 525. 1 416. 8 0. 0 941. 9

U S TOTA L 628. 2 

### 3 I 

# *: 8 944. 7 

### -SIZ E CLASS : 150-20 0 TABLE 2 7 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE

DCOST S (10** 6 198 2 $ )

BAS E
NAT . GAS RESI OOI L COA L TOTA L CAS E

NE UENG . 0. 0 14. 0 0. 0 14. 0

OPTIO N CAS E 1
NAT . GA S RESI DOI L COA L TOTA L NE

UENG . 0. 0 14. 0 0. 0 14. 0

OPTIO N CAS E 2
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 14. 3 0. 0 14. 3

OPTIO N CAS E 3
NAT . GAS RESI DOI L COA L TOTA L i NE UENG . 0. 0 14. 3 0. 0 14. 3

OPTIO N CAS E 4

• '

, NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 15. 1 0. 0 15. 1

OPTIO N CAS E 5
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 15. 1 0. 0 15. 1

OPTIO N CAS E 6
NAT . GAS RESI DOI L COA L TOTA L

I K. _ . NE UENG . 5. 0 10. 1 0. 0 15. 1 N

•

N

N

N

N

N

N Y

Y

.Y

.Y

.Y

Y

.Y ./N.J . 9. 9 17. 4 0. 0 27. 2

./N.J . 9. 9 17. 4 0. 0 27. 2

./N.J . 9. 9 17. 6 0. 0 27. 5

./N.J . 9. 9 17. 6 0. 0 27. 5

./N.J . 9. 9 18. 0 0. 0 27. 9

./N.J . 9. 9 18. 1 0. 0 27. 9

./N.J . 9. 9 18. 1 0. 0 28. 0 MI D

MID

MI D

MI D

MI D

MID

MI D . ATL . 12. 8 53. 4 0. 0 66. 2

. ATL . 12. 8 53. 4 0. 0 66. 2

. ATL . 12. 8 55. 5 0. 0 68. 2

. ATL . 12. 8 55. 5 0. 0 68. 2

. ATL . 15. 9 53. 2 0. 0 69. 0

. ATL . 15. 9 53. 2 0. 0 69. 1

. ATL . 15. 9 53. 5 0. 0 69. 4 SO

SO

S O

S O

SO

S O

S O . ATL . 0. 0 95. 5 0. 0 95. 5

. ATL . 0. 0 96. 3 0. 0 96. 3

. ATL . 0. 0 99. 9 0. 0 99. 9

. ATL . 0. 0 99. 9 0. 0 99. 9

. ATL . 0. 0 104. 6 0. 0 104. 6

. ATL . 0. 0 104. 7 0. 0 104. 7

. ATL . 0. 0 105. 7 0. 0 105. 7 MIDUES T

0. 0 112. 2 0. 0 112. 2

MIOUES T 0. 0 112. 7 0. 0 112. 7

MIDHES T 0. 0 117. 5 0. 0 117. 5

MIDUES T 0. 0 117. 5 0. 0 117. 5

MIDHES T 20. 0 100. 5 0. 0 120. 5

MIDUES T 20. 0 100. 6 0. 0 120. 6

MIDUES T 20. 0 101. 2 0. 0 121. 2 SO . HES T

105. 8 120. 8 0. 0 226. 6

SO . HES T 105. 8 123. 5 0. 0 229. 4

SO . UES T 234. 2 0. 0 0. 0 234. 2

SO . HES T 234. 2 0. 0 0. 0 234. 2

SO . UES T 234. 2 0. 0 0. 0 234. 2

SO . HES T 234. 2 0. 0 0. 0 234. 2

SO . HES T 234. 2 0. 0 0. 0 234. 2 CENTRA

L 0. 0 32. 9 0. 0 32. 9

CENTRA L 0. 0 33. 1 0. 0 33. 1

CENTRA L 33. 9 0. 0 0. 0 33. 9

CENTRA L 33. 9 0. 0 0. 0 33. 9

CENTRA L 33. 9 0. 0 0. 0 33. 9

CENTRA L 33. 9 0. 0 0. 0 33. 9

CENTRA L 33. 9 0. 0 0. 0 33. 9 NO .

NO .

NO .

NO .

NO .

NO .

NO . CNTR

L 21. 7 8. 8 6. 9 37. 4

CNTR L 21. 7 8. 8 7. 0 37. 5

CNTR L 30. 4 0. 0 7. 1 37. 5 "

CNTR L 37. 4 0. 0 0. 0 37. 4

CNTR L 37. 4 0. 0 0. 0 37. 4

CNTR L 37. 4 0. 0 0. 0 37. 4

CNTR L 37. 4 0. 0 0. 0 37. 4 HES T

9. 4 48. 3 0. 0 57. 7

HES T 9. 4 48. 3 0. 0 57. 7

UES T 9. 4 48. 3 0. 0 57. 7

HES T 9. 4 48. 3 0. 0 57. 7

HES T 9. 4 48. 6 0. 0 58. 0

UES T 9. 4 48. 6 0. 0 58. 0

HES T 48. 0 9. 5 0. 0 57. 5 N

O

N O

N O

N O

N O

N O

N O . HES T 0. 0 58. 7 0. 0 58. 7

, HES T 0. 0 58. 7 0. 0 58. 7

. UES T 0. 0 58. 7 0. 0 58. 7

. HES T 0. 0 58. 7 0. 0 58. 7

. UES T 0. 0 60. 2 0. 0 60. 2

. HES T 0. 0 60. 3 0. 0 60. 3

. HES T 0. 0 60. 7 0. 0 60. 7 U S TOTA

L 159. 6 561. 9 6. 9 728. 5

U S TOTA L 159. 6 566. 1 7. 0 732. 8

U S TOTA L 330. 5 411. 7 7. 1 749. 3

U S TOTA L 337. 5 411. 7 0. 0 749. 2

U S TOTA L 360. 5 400. 1 0. 0 760. 7

U S TOTA L 360. 5 400. 7 0. 0 761. 2

U S TOTA L 404. 1 

### 35 

# 8: 2 763. 0SIZ E CUSS : 200-25 0 TABL E 2 8 « INDUSTRIA L BOILE RNSP S REGIONA L IMPACT S B

YBOILE RSIZE , 1986-199 0
ANNUALIZE D COST S (10** 6 198 2 $ )

BAS E
NAT . GAS RESIOOI L COA L TOTA L CAS E

NE U ENG . 0. 0 6. 6 0. 0 6. 6

OPTIO N CAS E 1
NAT . GAS RESI DOI L COA L TOTA L NE

U ENG . 0. 0 6. 6 0. 0 6. 6

OPTIO N CAS E 2
NAT . GAS RESIDOI L COA L TOTA L NE

U ENG . 0. 0 6. 6 0. 0 6. 6

OPTIO N CAS E 3
NAT . GAS RESI DOI L COA L TOTA L NE

U ENG . 0. 0 6. 6 0. 0 6. 6

OPTIO N CAS E 4
NAT . GAS RESIDOI L COA L TOTA L NE

U ENG . 0. 0 6. 6 0. 0 6. 6

OPTIO N CAS E 5
NAT . GA S RESI DOI L COA L TOTA L NE

H ENG . 0. 0 6. 6 0. 0 6. 6

OPTIO N CAS E 6
NAT . GA S RESI DOI L COA L TOTA L NE

U ENG . 6. 4 0. 0 0. 0 6. 4 N

N

N

N

N

N

N Y

Y

Y

Y

Y

, Y

, Y ./N.J . 0. 0 12. 5 0. 0 12. 5

./N.J . 0. 0 12. 5 0. 0 12. 5

./N.J . 0. 0 12. 5 0. 0 12. 5

./N.J . 0. 0 12. 5 0. 0 12. 5

./N.J . 0. 0 12. 7 0. 0 12. 7

./N.J . 0. 0 12. 8 0. 0 12. 8

./N.J . 0. 0 12. 8 0. 0 12. 8 MID

MID

MI D

MI D

MID

MI D

MI D . ATL . 0. 0 43. 8 0. 0 43. 8

. ATL . 0. 0 43. 8 0. 0 43. 8

. ATL . 0. 0 44. 8 0. 0 44. 8

. ATL . 0. 0 44. 8 0. 0 44. 8

. ATL . 12. 6 32. 8 0. 0 45. 5

. ATL . 12. 6 32. 9 0. 0 45. 5

. ATL . 12. 6 33. 1 0. 0 45. 7 S O

S O

S O

SO

S O

S O

S O . ATL . 0. 0 59. 8 0. 0 59. 8

. ATL . 0. 0 59. 8 0. 0 59. 8

. ATL . 0. 0 61. 9 0. 0 61. 9

. ATL . 0. 0 61. 9 0. 0 61. 9

. ATL . 0. 0 64. 0 0. 0 64. 0

. ATL . 0. 0 64. 2 0. 0 64. 2

. ATL . 0. 0 64. 5 0. 0 64. 5 MIDUES T

0. 0 47. 2 29. 7 76. 9

MIDUES T 0. 0 75. 7 0. 0 75. 7

MIDHES T 0. 0 81. 0 0. 0 81. 0 .

MIDHES T 0. 0 81. 0 0. 0 81. 0

MIDHES T 0. 0 81. 3 0. 0 81. 3

MIDUES T 0. 0 81. 4 0. 0 81. 4

MIDHES T 0. 0 61. 9 0. 0 81. 9 SO . HES T

82. 3 91. 1 0. 0 173. 4

SO . HES T 82. 3 91. 1 0. 0 173. 4

SO . UES T 176. 6 0. 0 0. 0 176. 6

SO . HES T 176. 6 0. 0 0. 0 176. 6

SO . UES T 176. 6 0. 0 0. 0 176. 6

SO . HES T 176. 6 0. 0 0. 0 176. 6

SO . HES T 176. 6 0. 0 0. 0 176. 6 CENTRA

L 0. 0 13. 1 0. 0 13. 1

CENTRA L 0. 0 13. 1 0. 0 13. 1

CENTRA L 13. 4 0. 0 0. 0 13. 4

CENTRA L 13. 4 0. 0 0. 0 13. 4

CENTRA L 13. 4 0. 0 0. 0 13. 4

CENTRA L 13. 4 0. 0 0. 0 13. 4

CENTRA L 13. 4 0. 0 0. 0 13. 4 NO .

NO .

NO .

NO .

NO .

NO .

NO . CNTR

L 13. 6 0. 0 7. 2 20. 8

CNTR L 20. 4 0. 0 0. 0 20. 4

CNTR L 20. 4 0. 0 0. 0 20. 4

CNTR L 20. 4 0. 0 0. 0 20. 4

CNTR L 20. 4 0. 0 0. 0 20. 4

CNTR L 20. 4 0. 0 0. 0 20. 4

CNTR L 20. 4 0. 0 0. 0 20. 4 HES T

6. 1 14. 3 0. 0 20. 4

HES T 6. 1 14. 3 0. 0 20. 4

UES T 6. 1 14. 3 0. 0 20. 4

HES T 6. 1 14. 3 0. 0 20. 4

HES T 6. 1 14. 8 0. 0 20. 8

HES T 6. 1 14. 8 0. 0 20. 8

HES T 6. 1 14. 8 0. 0 20. 9 NO .

N O

N O

N O

N O

N O

N O HES T 0. 0 17. 9 0. 0 17. 9

HES T 0. 0 17. 9 0. 0 17. 9

. HES T 0. 0 17. 9 0. 0 17. 9

. HES T 0. 0 17. 9 0. 0 17. 9

. HES T 0. 0 18. 0 0. 0 18. 0

. HES T 0. 0 18. 0 0. 0 18. 0

. HES T 0. 0 

### l

# 8: l 18. 1 U S TOTA

L 102. 0 306. 4 36. 9 445. 3

U S TOTA L 108. 8 334. 9 0. 0 443. 7

U S TOTA L 216. 5 239. 1 0. 0 455. 6

U S TOTA L 216. 5 239. 1 0. 0 455. 6

U S TOTA L 229. 2 230. 3 0. 0 459. 5

U S TOTA L 229. 2 230. 7 0. 0 459. 8

U S TOTA L 235. 6 225. 2 0. 0 460. 8SIZE CUSS : > 25 0

BAS E
NAT . GAS RESI DOI L COA L TOTA L CAS E

NE UENG . 0. 0 14. 1 0. 0 14. 1

OPTIO N CAS E 1
NAT . GAS RESIDOI L COA L TOTA L NE

UENG . 0. 0 14. 1 0. 0 14. 1

OPTIO N CAS E 2
NAT . GAS RESIDOI L COA L TOTA L NE

UENG . 0. 0 14. 1 0. 0 14. 1

OPTIO N CAS E 3
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 0. 0 14. 1 0. 0 14. 1

OPTIO N CAS E 4
NAT . GAS RESI DOI L COA L TOTA L NE

W ENG . 5. 7 9. 2 0. 0 14. 9

OPTIO N CAS E 5
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 5. 7 9. 2 0. 0 14. 9

OPTIO N CAS E 6
NAT . GAS RESI DOI L COA L TOTA L NE

UENG . 5. 7 9. 3 0. 0 14. 9 N

N .

N .



### N

N

N

N TABL E 2 9 — INDUSTRIA

L BOILE R

Y

Y

Y

Y

Y

.Y

. Y ./N.J . 0. 0 37. 6 0. 0 37. 6

./N.J . 0. 0 37. 6 0. 0 37. 6

./N.J

. 0. 0 37. 6 0. 0 37. 6

./N.J . 0. 0 37. 6 0. 0 37. 6

./N.J . 11. 3 27. 4 0. 0 36. 7

./N.J . 11. 3 27. 5 0. 0 38. 8

./N.J . 11. 3 27. 5 

### 33: 8 MID . ATL .

11. 2 104. 2 0. 0 115. 4

MID . ATL . 11. 2 104. 2 0. 0 115. 4

MID . ATL . 11. 2 104. 2 0. 0 115. 4

MID . ATL . 11. 2 104. 2 0. 0 115. 4

MID . ATL . 25. 7 49. 3 44. 8 119. 7

MIO . ATL . 25. 7 49. 4 44. 8 119. 9

MID . ATL . 36. 4 38. 4 44. 9 119. 7 NSP S REGIONA L IMPACT S
ANNUALIZE

DCOST S

SO . ATL . 0. 0 176. 8 0. 0 176. 8

SO . ATL . 0. 0 176. 8 0. 0 176. 8

SO . ATL . 0. 0 176. 8 0. 0 176. 8

SO . ATL . 0. 0 176. 8 0. 0 176. 8

SO . ATL . 0. 0 187. 7 0. 0 187. 7

SO . ATL . 0. 0 186. 2 0. 0 188. 2

SO . ATL . 0. 0 189. 8 0. 0 189. 8 MIOUES T

0. 0 213. 3 0. 0 213. 3

MIDUES T 0. 0 213. 3 0. 0 213. 3

MIDHES T 0. 0 213. 3 0. 0 213. 3

MIDHES T 0. 0 213. 3 0. 0 213. 3

MIDHES T 85. 1 138. 0 0. 0 223. 1

MIDHES T 85. 1 63. 5 77. 5 226. 0

MIDHES T 96. 1 52. 2 77. 5 225. 8 (10** 6 198 2

SO . UES T 432. 1 0. 0 0. 0 432. 1

SO . UES T 432. 1 0. 0 0. 0 432. 1

SO . UES T 432. 1 0. 0 0. 0 432. 1

SO . HES T 432. 1 0. 0 0. 0 432. 1

SO . HES T 432. 1 0. 0 0. 0 432. 1

SO . HES T 432. 1 0. 0 0. 0 432. 1

SO . HES T 432. 1 0. 0 0. 0 432. 1 B

YBOILE R $ )

CENTRA L 19. 3 0. 0 26. 4 45. 7

CENTRA L 19. 3 O. O 26. 4 45. 7

CENTRA L 19. 3 0. 0 26. 4

. 45. 7

CENTRA L 44. 8 0. 0 0. 0 44. 8

CENTRA L 44. 8 0. 0 0. 0 44. 8

CENTRA L 44. 8 0. 0 0. 0 44. 8

CENTRA L 44. 8 0. 0 0. 0 44. 8 SIZ E

NO .

NO .

NO . \

NO .

NO .

NO .

NO . , 1986 -

CNTR L 38. 6 0. 0 22. 2 60. 8

CNTR L 38. 6 0. 0 22. 2 60. 6

CNTR L 38. 6 0. 0 22. 2 60. 8

CNTR L 38. 6 0. 0 24. 3 62. 9

CNTR L 38. 6 0. 0 24. 4 63. 0

CNTR L 38. 6 0. 0 24. 4 63. 0

CNTR L 38. 6 Z°'.b 63. 1 199 0

HES T 72. 4 18. 3 0. 0 90. 7

HES T 72. 4 18. 3 0. 0 90. 7

HES T 72. 4 18. 3 0. 0 90. 7

HES T 72. 4 18. 3 0. 0 90. 7

HES T 77. 8 13. 9 0. 0 91. 7

HES T 77. 8 13. 9 0. 0 91. 7

HES T 77. 8 13. 9 0. 0 91. 7 NO . UES T

0. 0 60. 5 27. 6 88. 1

NO . UES T 

### 6. 0 60. 5 27. 8 88. 2

NO . UES T 0. 0 60. 5 27. 8 86. 2

NO . UES T 0. 0 60. 5 27. 8 88. 2

NO . HES T 0. 0 63. 6 27. 9 91. 5

NO . HES T 0. 0 63. 7 27. 9 91. 6

NO . HES T 27. 5 36. 8 28. 0 92. 3 U S TOTA

L 573. 6 624. 7 76. 3 1274. 6

U S TOTA L 573. 6 624. 7 76. 4 1274. 7

U S TOTA L 573. 6 624. 7 76. 4 1274. 7

U S TOTA L 599. 1 624. 7 52. 1 1275. 9

U S TOTA L 721. 0 489. 1 97. 1 1307. 2

U S TOTA L 721. 0 415. 3 174. 6 1310. 9

U S TOTA L 770. 3 367. 9 175. 0 1313. 2 ' ~'*9^ ^



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