p. 1


# OAR Box 1865 Prepped byCharmelle Mathews



# Document

Number: 

# 118)IV-K-(B)-1 3 Docket Number: 

# A-83-2 7

Printed 12/3/20083:22:18PM

Sheet 118of 198

### f 

# A- 8 

# 3 P. 2 

# Li ENERGYAN

D ENVTOONMENTA

LANALYSIS , INC
. 165 5 NORT

HPOR T MYE RDRIV EARLINGTON

,VIRGINI

A 2220 9703/528-190 0IV-K-(B)-1 3



### January21 , 198 7

Mr . Rober t Pahel-Shor t Economi c Analysi s Branc h(MD-12 ) U.S . Environmenta l Protectio nAgency Researc hTriangl e Park , N C 2771 1 Subject : EPAContrac t No . 68-02-4202 , Wor k Assignmen t No . 1 8

Ne wIFCA

MRunResult s wit h198 4 Fue l Pric e Forecas t Dea r Robert : Enclose di s anIFCA Mbriefing packag e whic hsummarize s th e result s o f four ne wIFCA

Mruns . Th e IFCA

Msourc e code an

dalternative ai r emission s standard s ar e the sam e a s th e September/Octobe r 198 6 assump tions
. Th e fue l pric e forecas t i s EEA' s 198 4 Referenc e Pric e scenari o an dICF' s 198 3 coa l pric e projection
. Th e attache dtabl e present s a compariso no f thes e ne wIFCA Mrun s wit h198 4 IFCA

Mruns . Th e result s ar e similar
. Thes e incrementa l impact s ar e no t sensitive t o difference s i nassumption s relate dt o N0 X 

### emission s contro l costs , scrubbe r reductio no f PMemissions , an dth e applicabilit yo f th e curren t oi l SO 2 an dPMNSP S i nthe regulatory baseline
. Sincerely ,

Ti mHogan J TH:lm h enclosure s
cc : Dr . A . Weh e (withou t IFCA Mbriefing package )

MANAGEMENT / ECONOMIC S / ENGINEERIN GP. 3



## COMPARISON

OF IFCA

M PROJECTIONS 3



## 198 4 Results b

## 198 7 Results 0 

## Baselin e v . 0. 8 SO 2 emissio nred . (IO 3 

## shor t tons ) Tota l ann . cos t increas e ($198 5 IO 6 

## ) Incrementa l C- E(198 5 $/shor t ton ) 0. 8 v . G. 3 SOgemissio nred . (IO 3 

## shor t tons ) Tota l ann . cos t increas e ($198 5 IO 6 

## ) Incrementa l C- E(198 5 $/shor t ton ) 0. 3 v . al l scrub SO 2 emissio nred . (IO 3 

## shor t tons ) Tota l ann . cos t increas e ($198 5 IO 6 

## ) Incrementa l C- E(198 5 $/shor t ton ) Baselin e v . al l scrub SO 2 emissio nred . (IO 3 

## shor t tons ) Tota l ann . cos t increas e ($198 5 IO 6 

## ) Averag e C- E(198 5 $/shor t ton ) 

# 17 3 6 3 364
67 78 1,16 4


# 2 2 6 273
26 3 14 8 56 3 18

0 8 9 496
10 0 3 5 34 5
6 2 36 4
28 6 12 6 44 1

New industria l fossi l fuel-fire dboiler s large r than10 0 MMBtu/hr an d installe dbetwee n198 5 an d1990 . 198 4 EE

A Referenc e Pric e cas e oi l an dga s pric e forecas t an d198 3 ICF coa l pric e forecast . 198 4 assumptions . "Hig hOi l Demand " scenario . Projecte dImpact s o f Alternativ e Sulfu r Dioxid e New Sourc e Performanc e Standard s for Indus tria l Fossi l Fuel-Fire dBoilers . EEA . Marc h1985 . Baselin e an d alternativ e contro l level s II , I V an dVI . c 

## Januar y

198 7 results ; Fal l 198 6 assumptions .

# r r

c c t 

### ( 199 0 PROJECTE D NE WINDUSTRIA L FOSSI L FUEL-FIRE D BOILE R AI R EMISSIONS , FUE L DEMAND , AND COST S (198 6 IFCA M CODE . 198 4 REFERENCE FUE L PRICE S )
|lltMJLMllMMll:MJtMa t irwmnTinonHnnfj f

PREPARE D FOR : TH E U.S . ENVIRONMENTA L PROTECTIO N AGENC Y

PREPARE D BY : ENERG YAND ENVIRONMENTA L ANALYSIS , INC . 165 5 NORTH FOR

TMYE R DRIV E ARLINGTON . VIRGINI A2220 9

1/20/8 7

# I I
r r



# c
r c NOTE S O N IFCA M PROJECTION S

1 . 198 4 EE

A REFERENC EINDUSTRIA LOI LAN DGA S PRICEPROJECTION S ( 198 3 INDUSTRIA LCOALPRIC EPROJECTION S 2 . BAS ECAS E

- S02 : CURRENT COALNSPS ( ~ - PM : PROMULGATEDCOALNSP S (5 1 F R42769 )

- NOX : NOSIP'S , NONSP S 3 . OPTIO

N CAS E1 : ( ~ - COA LTYP EB , DIST . AN

D0. 8 PERCENT SULFU

RRESI DAR EI N

COMPLIANC E 4 . OPTIO

N CAS E2 :

- SCRUBAL LCOALTYPE S 9 0 PERCENT ( - DIST . AN D0. 3 PERCENT SULFU

RRESI DAREI N

COMPLIANCE 5 . OPTIO

N CAS E3 :

- SCRU BAL LCOALAN

DRESI DTYPE S 9 0 PERCENT

- DIST . I S IN

COMPLIANC E

TJ 6 i

# c\\ r r

r 

# c r
r

C 

# c c LIS T OF TABLE S

DESCRIPTIO

NO F TABL E TABL E NUMBE R
FUE L DEMAN

D

- NUMBE RO F UNIT S 1

- BTU S O F FUE L CONSUMPTIO N2 POLLUTAN

T EMISSION S 3 COST S 4 NOXONLY

- CONTRO L COST S 5

- EMISSIONS 6 NATIONA L IMPACT S B YSIZ E (MMBTU/HR 1

- 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
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 L FUE L DEMAN 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 D COST 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 9

b >

# I I

INDUSTRIAL BOILE RNE HSOURC E PERFORMANC E STANDARD S ASSUMPTION S OPTION CAS E 1 (AR021 3 )



### ( 

# r 

# r NATURAL GA S

30 2 CEILING(LB/MMBTU ) PM CEILING(LB/MMBTU ) NOXCEILING(LB/MMBTU ) DISTILLAT E FUE L OIL S0 2 CEILIN 6 (LB/MMBTU ) PM CEILING(LB/MMBTU ) NO XCEILING(LB/MMBTU ) RESIDUAL 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 )

- FO R<30 XC U NO XCEILING(LB/MMBTU ) 10-3 0 BOILERSIZ E CATEGORY(MMBTU/HRHEA 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
NONE NON E NONE
NON E NON E NON E
NON E NON E NON E NON E NON E

NON E NON E
NONE NONE NON E
NON E NON E NON E
NON E NON E NONE 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 NONE
NONE NONE NONE
NONE NONE NONE
NONE NONE NONE NONE NON E

NON E NONE
NONE NONE NONE
0.8 0 NON E NON E
1.2 0 0.0 5 0.2 0 NON E NON E

NON E NON E
NON E NON E NON E
0.8 0 NON E NON E
1.2 0 0.0 5 0.2 0 NON E NON E

NON E NON E
NON E NON E NON E
0.8 0 NON E NON E
1.2 0 0.0 5 0.2 0 NON E NON E

NON E NON E
NON E NON E NON E
0.8 0 NON E NON E
1.2 0 0.0 5 0.0 5 NON E

MANDATORYSCRUBBIN G REGULATION S



### ( 

# c c c RESIOUAL FUE L OI L

S0 2 FLOOR(LB/MMBTU ) PERCEN T S0 2 REMOVAL REQUIRE D MINIMU M PERCEN T S0 2 REMOVAL REQUIRE D LO USULFU REXEMPTION

(LB S02/MMBTU ) COAL S0 2 FLOOR(LB/MMBTU ) PERCEN T S0 2 REMOVAL REQUIRE D MINIMU M PERCEN T S0 2 REMOVAL REQUIRE D LOUSULFU

REXEMPTION

(L B S02/MMBTU ) NON E NON E NON E NON E
NON E NON E NON E NON E NONE

NONE NON E NON E
NON E NONE NON E NON E NON E

NON E NON E NON E
NON E NON E NON E NON E NONE

NONE NONE NONE
NONE NONE NONE NONE NONE

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

T l

### ( 

# r r

INDUSTRIA L BOILE RNE N SOURCE PERFORMANC

E STANDARD S ASSUMPTIONS OPTIO N CAS E 2 (AR021 4 ) 

# r 

# r c BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )

NATURA L GAS S0 2 CEILIN

G(LB/MMBTU ) P M CEILIN G(LB/MMBTU ) NO XCEILIN 6 (LB/MMBTU ) DISTILLATE FUE

L OI L 30 2 CEILIN

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

G(LB/MMBTU ) RESIDUA L FUE L OI L 30 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

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 30-5 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 50-7 5

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 75-10 0

NONE NONE NONE

NONE NONE NONE

NONE NONE NONE

NONE NONE NONE NONE 100-15 0

NON E NON E NON E

NON E NON E NON E
0.3 5 NON E NON E
1.2 0 0.0 5 0.2 0 NON E 150-20 0

NON E NON E NON E

NON E NON E NON E
0.3 5 NON E NON E
1.2 0 0.0 5 0.2 0 NONE 200-25 0

NON E NON E NON E

NON E NON E NON E
0.3 5 NON E NON E
1.2 0 0.0 5 0.2 0 NON E >25 0

NON E NON E NON E

NON E NON E NON E
0.3 5 NON E NON E
1.2 0 0.0 5 0.0 5 NON E

MANDATOR

YSCRUBBIN

GREGULATIONS 

### ( 

# c RESIDUA L FUE L OI L S0 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T 30 2 REMOVA

L REQUIRE

D LO HSULFU REXEMPTIO

N (L B S02/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 HSULFU REXEMPTIO

N (L B S02/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 NONE

NONE NONE NONE

NONE NONE NONE NONE NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E NON E

NON E NON E NON E

NON E 90.0 0 NON E NON E

T l 0 0

# I I

INDUSTRIA L BOILE RNEHSOURCE PERFORMANC E STANDARDS ASSUMPTIONS OPTIO N CAS E 3 (AR021 2 )
BOILE RSIZ E CATEGOR

Y(MMBTU/H

RHEA T INPUT )



# r r r NATURA L GAS S0 2 CEILIN

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

G(LB/MMBTU ) DISTILLATE FUE

L OI L S0 2 CEILIN

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

G(LB/MMBTU ) RESIDUA L FUEL OI L 30 2 CEILIN

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

G(LB/MMBTU ) COA L 30 2 CEILIN

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

- FO R<30 XC

U NO XCEILIN

G(LB/MMBTU ) 10-3 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 30-5 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 50-7 5

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 75-10 0

NONE NONE NON E

NONE NON E NONE

NON E NON E NON E

NON E NONE NONE NONE 100-15 0

NON E NON E NON E

NON E NON E NON E
0.8 0 NON E NON E
1.2 0 0.0 5 0.2 0 NON E 150-20 0

NON E NON E NON E

NON E NON E NONE
0.8 0 NON E NON E
1.2 0 0.0 5 0.2 0 NON E 200-25 0

NON E NON E NON E

NON E NON E NON E
0.6 0 NON E NON E
1.2 0 0.0 5 0.2 0 NON E >25 0

NON E NON E NON E

NON E NON E NON E
0.8 0 NON E NON E
1.2 0 0.0 5 0.0 5 NON E

MANDATOR

YSCRUBBIN

GREGULATIONS



# c c c RESIDUA L FUEL OI L 30 2 FLOO

R(LB/MMBTU ) PERCEN T S0 2 REMOVA

L REQUIRE

D MINIMU M PERCEN T S0 2 REMOVA

L REQUIRE

D LO HSULFU REXEMPTIO

N (L B S02/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 HSULFU REXEMPTIO

N (L B S02/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 NONE

NON E NON E NONE

NONE NONE NON E NON E NON E

90.0 0 NON E NON E

NON E 90.0 0 NON E NON E NON E

90.0 0 NON E NON E

NON E 90.0 0 NON E NON E NON E

90.0 0 NON E NON E

NON E 90.0 0 NON E NON E NON E

90.0 0 NON E NON E

NON E 90.0 0 NON E NON E

T l C O( TABL E 1 — 199 0 FUEL DEMAN

D (NUMBE ROF UNITS ) BOILE RSIZ E (MMBTU/HR ) p10-5 0 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L 

# r
r



# r c

( 

# c 

# c

r •TOTAL * TH E BAS E OPTIO N OPTIO N OPTIO N NATURA L GAS TH E BAS E OPTIO N OPTIO N OPTIO N COA L TH E BAS E CAS E CAS E 1 CAS E 2 CAS E 3 AN DOI L CAS E CAS E 1 CAS E 2 CAS E 3
CAS E OPTIO N CAS E 1 OPTIO N OPTIO N CAS E 2 CAS E 3 1412 .

1412 . 1412 . 1412 . 1371 . 1371 . 1371 . 1371 . 41 . 41 . 41 . 41 . 577 .

577 . 577 . 577 . 552 . 552 . 552 . 552 . 25 . 25 . 25 . 25 . 271 .

271 . 271 . 271 . 265 . 267 . 271 . 271 . 6 . 4 . 0 . 0 . 135 .

135 . 135 . 135 . 134 . 134 . 135 . 135 . 1 . 1 . 0 . 0 . 62 .

62 . 62 . 62 . 59 . 59 . 62 . 62 . 3 . 3 . 0 . 0 . 136 .

136 . 136 . 136 . 124 . 124 . 134 . 134 . 12 . 12 . 2 . 2 . 2593 . 2593 . 2593 . 2593 . 2505 . 2507 . 2525 . 2525 . 88 . 86 . 68 . 68 .

T l o

# c r r 

# r c r S0 2 10-5 0 TABLE 3 — 199 0 EMISSIONS (10*« 3 TONS ) 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 CAS E OPTION CAS E OPTION CAS E OPTION CAS E P M TH E BAS E CAS E OPTION CAS E OPTION CAS E OPTION CAS E NO X TH E BAS E CAS E OPTIO N CAS E OPTION CAS E OPTION CAS E PM1 0 TH E BAS E CAS E OPTION CAS E OPTION CAS E OPTION CAS E 1 2 3

. 1 2 3

1 2 3

1 2 3 117 .

117 . 117 . 117 .
11 . 11 . 11 . 11 .
21 . 21 . 21 . 21 .
10 . 10 . 10 . 10 . 118 .

118 . 118 . 118 .
11 . 11 . 11 . 11 .
24 . 24 . 24 . 24 .
10 . 10 . 10 . 10 . 119 .

38 . 14 . 12 .
9 . 4 . 4 . 4 .
25 . 20 . 20 . 21 .
9 . 4 . 4 . 4 . 92 .

34 . 15 . 14 .
7 . 4 . 4 . 4 .
22 . 22 . 22 . 22. .
7 . 4 . 4 . 4 . 66 .

26 . 9 . 8 .
5 . 3 . 3 . 3 .
15 . 16 . 13 . 13 .
5 . 3 . 3 . 3 . 70 .

70 . 30 . 28 .
7 . 7 . 8 . 8 .
33 . 33 . 30 . 30 .
7 . 7 . 8 . 8 . 582 .

403 . 303 . 296 .
50 . 41 . 41 . 41 .
139 . 136 . 130 . 131 .
48 . 40 . 39 . 39 .



### ( 

# c c c

# rl l c r
r 

# r r c

c c c c •TOTAL * TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E NATURA L GAS TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E 1 2 3

1 2 3 RESIDUA L FUEL.OI L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2 OPTIO N CAS E 3 COA L TH E BAS E CAS E OPTIO N CAS E OPTIO N CAS E OPTIO N CAS E 1 2 3 10-5 0

132 . 132 . 132 . 132 . 28 . 28 . 28 . 28 . 93 . 93 . 93 . 93 . 11 . 11 . 11 . 11 . TABLE 2 —

199 0 FUE

L DEMAN D (10**1 2 BTUS ) BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L
136 . 136 . 136 . 136 . 24 . 24 . 24 . 24 . 102 . 102 . 102 . 102 . 10 . 10 . 10 . 10 . 129 .

129 . 129 . 129 . 10 . 30 . 46 . 52 . 114 . 96 . 83 . 77 . 4 . 3 . 0 . 0 . 

### Ill

11 1 11 1 11 1
1 2 2 6 2 7 2 7
9 8 8 5 8 4 8 4
1 1 0 0 67 .

67 . 67 . 67 . 0 . 0 . 17 . 17 . 64 . 64 . 50 . 50 . 191 .

191 . 191 . 191 . 17 . 17 . 17 . 17 . 149 . 149 . 170 . 170 . 25 . 25 . 4 . 4 . 766 .

766 . 766 . 766 . 91 . 124 . 158 . 163 . 620 . 589 . 583 . 577 . 55 . 53 . 25 . 25 .

T l

# c\\ r r

(~TABL E 4 —199 0 COST S (10«*6 . «1985 ) BOILE RSIZ E (MMBTU/HR ) /

- 10-5 0 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L ANNUALIZE D COST S - TOTA L 

# c r

c c ! 

# c TH E BAS E CAS E OPTIO N CAS E I OPTIO N CAS E 2 OPTIO N CAS E 3 CAPITA L COST S TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2 OPTIO N CAS E 3 1357. 0

1357. 0 1357. 0 1357. 0 TOTA L 1482. 9 1482. 9 1482. 9 1482. 9 1164. 5

1164. 5 1164. 5 1164. 5
1307. 7 1307. 7 1307. 7 1307. 7 988. 3

1027. 0 1039. 6 1040. 9
905. 7 898. 9 875. 2 894. 7 797. 8

827. 2 832. 3 832. 6
579. 7 617. 4 601. 1 601. 2 487. 3

508. 3 509. 5 509. 7
391. 1 421. 6 346. 9 346. 9 1417. 6

1417. 6 1433. 2 1433. 9
1234. 4 1234. 4 1039. 8 1040. 0 6212. 4

6301. 6 6336. 1 6338. 5
5901. 6 5963. 0 5653. 6 5673. 4

# r 

# I I

10-5 0 TABLE 5 — 199 0 NO

XCONTRO L ANNUALIZE D COST S (10*»6 . 91985 ) BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 

# f 

# c c c TOTA L •TOTAL * TH E BAS E CAS E OPTION CAS E 1 OPTIO N CAS E 2 OPTIO N CAS E 3 NATURAL GA S ANDOI L TH E BAS E CAS E OPTIO N CAS E 1 OPTION CAS E 2 OPTIO N CAS E 3 COAL TH E BAS E CAS E OPTION CAS E 1 OPTION CAS E 2 OPTIO N CAS E 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
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. 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

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. 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 0. 0 0. 0



# c c c c

# r r r



# r r c c r *TOTAL« TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2 OPTIO N CAS E 3 NATURA L 6AS AN

DOI L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2 OPTIO N CAS E 3 COA L TH E BAS E CAS E OPTIO N CAS E 1 OPTIO N CAS E 2 OPTIO N CAS E 3 10-5 0 TABL E 6 ~ 199 0 NO

XEMISSIONS (10** 3 TONS ) BOILE RSIZ E (MMBTU/HR ) 50-10 0 100-15 0 150-20 0 200-25 0 > 25 0 TOTA L 21. 1 21. 1 21. 1 21. 1 18. 9 18. 9 18. 9 18. 9
2. 2 2. 2 2. 2 2. 2 24. 0

24. 0 24. 0 24. 0 20. 8 20. 8 20. 8 20. 8
3. 2 3. 2 3. 2 3. 2 24. 5

20. 0 20. 4 21. 3 23. 1 19. 1 20. 4 21. 3
1. 4 0. 9 0. 0 0. 0 21. 6

22. 3 22. 0 22. 0 21. 2 21. 9 22. 0 22. 0
0. 4 0. 4 0. 0 0. 0 15. 0

15. 7 13. 4 13. 4 13. 5 14. 2 13. 4 13. 4
1. 5 1. 5 0. 0 0. 0 33. 3

33. 3 29. 5 29. 5 24. 4 24. 4 28. 1 28. 1
8. 9 8. 9 1. 4 1. 4 139. 3

136. 1 130. 3 131. 3 121. 8 119. 1 123. 5 124. 5 17. 5 17. 0 6. 8 6. 8 

### ( 

# c c r

# r 

# I I

( 

# r r r 

# r r r c c TABL E 7 —INDUSTRIA L BOILE RNSP S NATIONA L IMPACT S B

YBOILE RSIZE , 1986-199 0



# c c c BOILE RSIZ E (MMBTU/HR )

10-5 0
FUE L DEMAN

D (NUMBE ROF UNITS ) NATURAL 6A S AN

D OI L COAL "TOTAL * FUE L DEMAN

D (10**1 2 BTUS ) NATURAL 6A S DISTILLAT E FUE L OI L RESIDUA L FUE L OI L COAL "TOTAL * EMISSIONS (10** 3 TONS ) 30 2 PM NO X PM1 0 EMISSIONS ( XCHANGE FRO

MBAS E CASE ) S0 2 P M NOX PM1 0 ANNUALIZE D COST S (10**6 , -H985 ) BOILE R FG D AN D PM NOX FUE L •TOTAL * ANNUALIZE D COST S ( XCHANGE FRO

MBAS E CASE ) *TOTAL * CAPITA L COST S (10**6 , 41985 ) BOILE R FG D AN D PM NO X •TOTAL * THE BAS E OPTIONOPTIO NOPTIO

N CAS E CAS E 1 CAS E 2 CAS E 3

1371 . 1371 . 1371 . 1371 . 

### 41 . 41 . 41 . 41 . 1412 . 1412 . 1412 . 1412 .
28 . 0 . 93 . 1 1 . 132 .
116. 9 10. 8 21. 1 9. 9

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

656. 4 5. 4 0. 0 695. 2 1357. 0 28 .

0 . 93 . 1 1 . 132 .
116. 9 10. 8 21. 1 9. 9

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

656. 4 5. 4 0. 0 695. 2 1357. 0 28 .

0 . 93 . 1 1 . 132 .
116. 9 10. 8 21. 1 9. 9

0. 0 0. 0 0. 0 O. O

656. 4 5. 4 0. 0 695. 2 1357. 0 28 .

0 . 93 . 1 1 . 132 .
116. 9 10. 8 21. 1 9. 9

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

656. 4 5. 4 0. 0 695. 2 1357. 0

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

1471 . 12 . 0 . 1483 . 1471 .

12 . 0 . 1483 . 1471 .

12 . 0 . 1483 . 1471 .

12 . 0 . 1483 .
T l

# cll r

TABL E 8 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0



# c r r r

c c BOILE RSIZ E (MMBTU/HR ) 50-7 5
FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L *TOTAL « FUEL DEMAN

D (10**1 2 BTUS ) NATURA L 6AS DISTILLAT E FUEL OI L RESIDUA L FUEL OI L COA L *TOTAL « EMISSIONS (10»* 3 TONS ) 30 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10»*6 , 91985 ) BOILE R F6 DAN DP M NO X FUEL •TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) *TOTAL« CAPITA L COST S (10**6 . 01985 ) BOILE R FG DAN DP M NO X •TOTAL * TH E BAS E CAS E

389 . 13 . 402 .

14 . 0 . 64 . 5 . 83 .

71. 7 6. 4 14. 3 6. 0

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

281. 3 6. 7 0. 0 435. 7 723. 7 OPTIO

N CAS E 1

389 . 13 . 402 .

14 . 0 . 64 . 5 . 83 .

71. 7 6. 4 14. 3 6. 0

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

281. 3 6. 7 0. 0 435. 7 723. 7 OPTIO

N CAS E 2

389 . 13 . 402 .

14 . 0 . 64 . 5 . 83 .

71. 7 6. 4 14. 3 6. 0

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

281. 3 6. 7 0. 0 435. 7 723. 7 OPTIO

N CAS E 3

389 . 13 . 402 .

14 . 0 . 64 . 5 . 83 .

71. 7 6. 4 14. 3 6. 0

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

281. 3 6. 7 0. 0 435. 7 723. 7

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

802 . 14 . 0 . 816 . 802 .

14 . 0 . 816 . 802 .

14 . 0 . 816 . 802 .

14 . 0 . 816 .
T l

# r

r 

# r r TABL E 9 ~ INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0



# c c r
r BOILE RSIZ E (MMBTU/HR ) 75-10 0
FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L 6AS AN

DOI L COA L "TOTAL * FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS DISTILLATE FUEL OI L RESIDUA L FUEL OI L COA L *TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X FUEL •TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * CAPITA L COST S (10**6 . 91985 ) BOILE R FG DAN DP M NO X •TOTAL * TH E BAS E CAS E

163 . 12 . 175 .

10 . 0 . 39 . 5 . 54 .

46. 2 4. 8 9. 7 4. 4

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

159. 1 5. 4 0. 0 276. 3 440. 8 OPTIO

N CAS E 1

163 . 12 . 175 .

10 . 0 . 39 . 5 . 54 .

46. 2 4. 8 9. 7 4. 4

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

159. 1 5. 4 0. 0 276. 3 440. 8 OPTIO

N CAS E 2

163 . 12 . 175 .

10 . 0 . 39 . 5 . 54 .

46. 2 4. 8 9. 7 4. 4

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

159. 1 5. 4 0. 0 276. 3 440. 8 OPTIO

N CAS E 3

163 . 12 . 175 .

10 . 0 . 39 . 5 . 54 .

46. 2 4. 8 9. 7 4. 4

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

159. 1 5. 4 0. 0 276. 3 440. 8



### 0. 0 0. 0 0. 0 0. 0

480 . 12 . 0 . 492 . 480 .

12 . 0 . 492 . 480 .

12 . 0 . 492 . 480 .

12 . 0 . 492 .

T l 0 0

# r r r r 

# C C 

# c TABLE 1 0 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0



# C 

# r c c BOILE RSIZ E (MMBTU/HR ) 100-15 0
FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L 6AS AN

DOI L COA L *TOTAL * FUE L DEMAN D (10**1 2 BTUS ) NATURA L 6AS DISTILLATE FUE

L OI L RESIDUA L FUE L OI L COA L *TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X FUEL •TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) •TOTAL * CAPITA L COST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X *TOTAL * THE BAS E CAS E

265 . 6 . 271 .

10 . 0 . 114 . 4 . 129 .

119. 3 8. 6 24. 5 8. 6

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

283. 4 26. 2 0. 0 678. 8 988. 3 OPTIO

N CAS E 1

267 . 4 . 271 .

30 . 0 . 96 . 3 . 129 .

38. 0 4. 4 20. 0 4. 4

-68. 1 -48. 8 -18. 4 -48. 8

279. 2 38. 5 0. 0 709. 3 1027. 0 OPTIO

N CAS E 2

271 . 0 . 271 .

46 . 0 . 83 . 0 . 129 .

14. 2 3. 9 20. 4 3. 9

-88. 1 -54. 7 -16. 7 -54. 7

270. 6 51. 4 0. 0 717. 6 1039. 6 OPTIO

N CAS E 3

271 . 0 . 271 .

52 . 0 . 77 . 0 . 129 .

12. 4 4. 0 21. 3 4. 0

-89. 6 -53. 5 -13. 1 -53. 5

270. 5 61. 0 0. 0 709. 4 1040. 9



### 0. 0 3. 9 5. 2 5. 3

854 . 52 . 0 . 906 . 835 .

64 . 0 . 899 . 796 .

79 . 0 . 675 . 79 5

10 0 0 89 5

Tl C D

# r I I

TABLE 11 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE . 1986-199 0 

# c c r r

C 

# c
r
r
( 

# C 

# c c BOILE RSIZ E (MMBTU/HR ) 150-20 0
FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L *TOTAL * FUE L DEMAN D (10**1 2 BTUS ) NATURA L GAS DISTILLATE FUEL OI L RESIDUA L FUEL OI L COA L *TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 , 91985 ) BOILE R F6 DAN DP M NO X FUE L *TOTAL» ANNUALIZE

DCOST S ( XCHANG

E FRO HBAS E CASE ) •TOTAL * CAPITA L COST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X •TOTAL * TH E BAS E CAS E

134 . 1 . 135 .
12 . 0 . 98 . 1 . U l .
92. 1 6. 7 21. 6 6. 7

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

179. 1 27. 5 0. 0 591. 2 797. 8 OPTIO N

CAS E 1

134 . 1 . 135 .
26 . 0 . 85 . 1 . U l .
33. 5 4 . 1 22. 3 4 . 1

-63. 6 -38. 8 3. 2 -38. 8

179. 0 54. 9 0. 0 593. 4 827. 2 OPTIO N

CASE 2

135 . 0 . 135 .
27 . 0 . 84 . 0 . 111 .
14. 7 4. 1 22. 0 4. 1

-84. 0 -38. 8 1. 9 -38. 8

175. 2 59. 1 0. 0 598. 0 832. 3 OPTIO N

CAS E 3

135 . 0 . 135 .
27 . 0 . 64 . 0 . U l .
13. 5 4 . 1 22. 0 4 . 1

-85. 3 -38. 8 1. 9 -38. 8

175. 2 59. 4 0. 0 598. 0 632. 6

0. 0 3. 7 4. 3 4. 4

529 . 5 0 . 0 . 580 . 529 .

69 . 0 . 617 . 513 .

88 . 0 . 601 . 513 .

8 8 . 0 . 601 .

T l

# r c r TABL E 1 2 —INDUSTRIA L BOILE R NSPS NATIONA L IMPACTS B YBOILE R SIZE . 1986-199 0



# c c c

c c c r BOILE RSIZ E (MMBTU/HR ) 200-25 0
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 FUEL OI L RESIDUA L FUEL OI L COA L *TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X FUEL •TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) *TOTAL * CAPITA L COST S (10**6 . 91985 ) BOILE R FG DAN DP M NO X *TOTAL * TH E BAS E CAS E

59 . 3 . 62 .

0 . 0 . 64 . 3 . 67 .

65. 9 4. 9 15. 0 4. 9

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

124. 7 19. 6 0. 0 342. 7 487. 3 OPTIO

N CAS E 1

59 . 3 . 62 .

0 . 0 . 64 . 3 . 67 .

26. 3 3. 2 15. 7 3. 2

-60. 1 -34. 7 4. 7 -34. 7

124. 7 41. 5 0. 0 342. 1 508. 3 OPTIO

N CAS E 2

62 . 0 . 62 .

17 . 0 . 50 . 0 . 67 .

6. 8 2. 6 13. 4 2. 6

-66. 6 -46. 9 -10. 7 -46. 9

113. 2 33. 3 0. 0 362. 9 509. 5 OPTIO

N CAS E 3

62 . 0 . 62 .

17 . 0 . 50 . 0 . 67 .

6. 1 2. 6 13. 4 2. 6

-87. 7 -46. 9 -10. 7 -46. 9

113. 2 33. 5 0. 0 362. 9 509. 7

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

353 . 36 . 0 . 391 . 353 .

69 . 0 . 422 . 300 .

47 . 0 . 347 . 300 .

47 . 0 . 347 . 

# c T l ho

# r

TABL E 1 3 — INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0



### ( 

# r c 

# c

c c c BOILE RSIZ E (MMBTU/HR ) > 25 0
FUEL DEMAN

D (NUMBE RO F UNITS ) NATURA L GA S AN DOI L COA L *TOTAL * FUE L DEMAN D (10**1 2 BTUS ) NATURA L 6AS DISTILLATE FUE

L OI L RESIDUA L FUE L OI L COA L *TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 . 91985 ) BOILE R FG OAN DP M NO X FUE L •TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) *TOTAL * CAPITA L COST S (10**6 . 91985 ) BOILE R FG DAN DP M NO X •TOTAL * TH E BAS E CAS E

124 . 12 . 136 .

17 . 0 . 149 . 25 . 191 .

69. 9 7. 4 33. 3 7. 4

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

370. 3 68. 1 0. 0 959. 2 1417. 6 OPTIO

N CAS E 1

124 . 12 . 136 .

17 . 0 . 149 . 25 . 191 .

69. 9 7. 4 33. 3 7. 4

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

370. 3 66. 1 0. 0 959. 2 1417. 6 OPTIO

N CAS E 2

134 . 2 . 136 .

17 . 0 . 170 . 4 . 191 .

30. 1 6. 2 29. 5 8. 2

-56. 9 10. 8 -11. 4 10. 8

321. 7 112. 8 0. 0 998. 6 1433. 2 OPTIO

N CAS E 3

134 .Ol 136 .

17 . 0 . 170 . 4 . 191 .

27. 6 8. 2 29. 5 8. 2

-60. 5 10. 8 -11. 4 10. 8

321. 7 113. 5 0. 0 998. 6 1433. 9



### 0. 0 0. 0 1. 1 1. 1

1091 . 144 . 0 . 1234 . 1091 .

144 . 0 . 1234 . 880 .

160 . 0 . 1040 . 880 .

160 . 0 . 1040 .

# r r r 

# c c r

c c c TABLE 1 4 INDUSTRIA L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE . 1986-199 0
BOILE RSIZ E (MMBTU/HR ) > 10 0
FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

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

L OI L RESIDUA L FUEL OI L COA L •TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X FUEL •TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL * CAPITA L COST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X. •TOTAL * TH E BASE CASE

562 . 22 . 604 .
39 . 0 . 425 . 34 . 498 .
347. 2 27. 6 94. 4 27. 6

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

957. 5 161. 6 0. 0 2571. 9 3691. 0 OPTIO N

CAS E 1

90*r * 20 . 604 .

72 . 0 . 393 . 33 . 498 .
167. 7 19. 1 91. 3 19. 1

-51. 7 -30. 8 -3. 3 -30. 8

953. 2 223. 0 0. 0 2603. 9 3780. 1 OPTIO N

CAS E 2

602 . 2 . 604 .
106 . 0 . 388 . 4 . 498 .
67. 8 18. 6 85. 3 18. 8

-80. 5 -31. 9 -9. 6 -31. 9

880. 8 256. 6 0. 0 2677. 2 3814. 6 OPTIO N

CAS E 3

602 . 2 . 604 .

112 . 0 . 382 . 4 . 498 .
61. 6 18. 9 86. 2 18. 9

-82. 3 -31. 5 -8. 7 -31. 5

880. 6 267. 4 0. 0 2669. 0 3817. 0

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

2626 . 283 . 0 . 3111 . 2607 .

365 . 0 . 3172 . 2489 .

374 . 0 . 2863 . 2468 .

394 . 0 . 2883 . 

# c

## r

TABL E 1 5 INDUSTRIA L BOILE RNSP S NATIONA L IMPACT S B

YBOILE RSIZE . 1986-199 0



# c c c

c c c c BOILE RSIZ E (MMBTU/HR )

100-25 0
FUE L DEMAN

D (NUMBEROF UNITS ) NATURAL GA 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 RESIDUAL FUE L OI L COAL "TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NOX PM1 0 EMISSIONS ( XCHANGE FRO

MBAS E CASE ) 30 2 PM NOX PM1 0 ANNUALIZE D COST S (10**6 , 91985 ) BOILE R FG D AN D PM NOX FUE L •TOTAL * ANNUALIZE D COST S ( XCHANGE FRO

MBAS E CASE ) *TOTAL « CAPITA L COST S (10**6 , 91985 ) BOILE R FG D AN D PM NOX •TOTAL * TH E BAS E CAS E

456 . 10 . 468 .
23 . 0 . 275 . 9 . 307 .

277. 3 20. 2 61. 1 20. 2

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

587. 2 73. 5 0. 0 1612. 7 2273. 4 OPTIO N

CAS E 1

460 . 8 . 468 .
55 . 0 . 244 . 7 . 307 .
97. 8 11. 7 58. 0 11. 7

-64. 7 -42. 1 -5. 1 -42. 1

582. 9 134. 9 0. 0 1644. 7 2362. 5 OPTIO N

CASE 2

468 . 0 . 468 .
90 . 0 . 217 . 0 . 307 .
37. 7 10. 6 55. 8 10. 6

-86.4 - -47. 5 -8. 7 -47. 5

559. 0 143. 8 0. 0 1678. 6 2381. 4 OPTIO N

CASE 3

468 . 0 . 468 .
95 . 0 . 212 . 0 . 307 .
34. 0 10. 7 56. 7 10. 7

-87. 7 -47. 0 -7. 2 -47. 0

558. 9 153. 9 0. 0 1670. 4 2383. 2



### 0. 0 3. 9 4. 7 4. 6

1737 . 140 . 0 . 1877 . 1717 .

221 . 0 . 1938 . 1609 .

214 . 0 . 1823 . 160 8

23 5 0 184 3

r o

# r c TABL E 1 6 INDUSTRIA L BOILE R NSPS NATIONA L IMPACTS B YBOILE R SIZE , 1986-199 0



# r r c c

c c BOILE RSIZ E (MMBTU/HR ) > 5 0
FUE L DEMAN D (NUMBE RO F UNITS ) NATURA L GAS AN

DOI L COA L •TOTAL * FUEL DEMAN

D (10**1 2 BTUS ) NATURA L 6AS DISTILLATE FUE

L OI L RESIDUA L FUEL OI L COA L *TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 , 91985 ) BOILE R FG OAN DP M NO X FUEL •TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL * CAPITA L COST S (10**6 , 91985 ) BOILE R FG OAN DP M NO X "TOTAL " I E BAS E CAS E

1134 . 47 . 1181 .

63 . 0 . 527 . 44 . 634 .
465. 1 38. 8 118. 4 38. 0

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

1397. 9 173. 6 0. 0 3283. 9 4855. 5 OPTIO

N CAS E 1

1136 . 45 . 1181 .
96 . 0 . 496 . 43 . 634 .
285. 6 30. 3 115. 3 29. 5

-38. 6 -21. 9 -2. 6 -22. 4

1393. 6 235. 1 0. 0 3315. 9 4944. 6 OPTIO

N CAS E 2

1154 . 27 . 1181 .
130 . 0 . 490 . 14 . 634 .
185. 7 30. 0 109. 3 29. 2

-60. 1 -22. 7 -7. 7 -23. 2

1321. 2 268. 7 0. 0 3389. 2 4979. 1 OPTION

CAS E 3

1154 . 27 . 1181 .
136 . 0 . 484 . 14 . 634 .
179. 5 30. 1 110. 2 29. 3

-61. 4 -22. 4 -6. 9 -22. 9

1321. 0 279. 5 0. 0 3381. 0 4981. 5



### 0. 0 1. 8 2. 5 2. 6

4110 . 309 . 0 . 4419 . 4090 .

390 . 0 . 4460 . 3771 .

399 . 0 . 4171 . 3770 .

420 . 0 . 4190 .

# r c r c r c r c TABL E 1 7 INDUSTRIA

L BOILE RNSP S NATIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0



# c c c r BOILE RSIZ E (MMBTU/HR ) TOTA L
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 DISTILLAT E FUEL OI L RESIDUA L FUEL OI L COA L «TOTAL * EMISSIONS (10** 3 TONS ) S0 2 P M NO X PM1 0 EMISSIONS ( XCHANG

E FRO M BAS E CASE ) S0 2 P M NO X PM1 0 ANNUALIZE

DCOST S (10**6 . 91985 ) BOILE R FG OAN DP M NO X FUE L *TOTAL * ANNUALIZE

DCOST S ( XCHANG

E FRO M BAS E CASE ) "TOTAL * CAPITA L COST S (10**6 , 91985 ) BOILE R FG DAN DP M NO X •TOTAL " TH E BAS E CAS E

2505 . 68 . 2593 .
91 . 0 . 620 . 55 . 766 .

582. 0 49. 5 139. 3 47. 9

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

2054. 4 179. 1 0. 0 3979. 0 6212. 4 OPTIO

N CAS E 1

2507 . 86 . 2593 .

124 . 0 . 589 . 53 . 766 .

402. 5 41. 1 136. 1 39. 5

-30. 8 -17. 0 -2. 3 -17. 5

2050. 0 240. 5 0. 0 4011. 0 6301. 6 OPTIO

N CAS E 2

2525 . 68 . 2593 .

158 . 0 . 583 . 25 . 766 .

302. 6 40. 6 130. 3 39. 1

-48. 0 -17. 6 -6. 5 -18. 4

1977. 6 274. 1 0. 0 4084. 3 6336. 1 OPTIO

N CAS E 3

2525 . 68 . 2593 .

163 . 0 . 577 . 25 . 766 .

296. 3 40. 9 131. 3 39. 3

-49. 1 -17. 4 -5. 7 -18. 0

1977. 5 284. 9 0. 0 4076. 1 6338. 5



### 0. 0 1. 4 2. 0 2. 0

5581 . 321 . 0 . 5902 . 5561 .

402 . 0 . 5963 . 5242 .

411 . 0 . 5654 . 5241 .

432 . 0 . 5673 .

# cll r 

# r r r 

# c c r SIZ E CLASS : 100-15 0

BAS E CAS E NE N ENG . NAT . GAS 0. 0 RESI DOI L 1189. 0 COA L 0. 0 TOTA L 1189. 0



# C 

# c c OPTIO N CAS E 1 NE N ENG . NAT . 6AS 0. 0 RESI DOI L 941. 0 COA L 0. 0 TOTA L 941. 0
OPTIO N CAS E 2 NE N EN6 . NAT . 6A S 0. 0 RESI DOI L 449. 0 COA L 0. 0 TOTA L 449. 0
OPTIO N CAS E 3 NE HENG . NAT . 6AS 0. 0 RESI DOI L 211. 0 COA L 0. 0 TOTA L 211. 0 TABLE 1 8 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0 30 2 EMISSIONS (SHOR T TONS )

N

N

N

N .Y./N.J . 0. 0 1624. 0 0. 0 1824. 0

.Y./N.J . 0. 0 1105. 0 0. 0 1105. 0

.Y./N.J . 0. 0 460. 0 0. 0 460. 0

.Y./N.J . 0. 0 422. 0 0. 0 422. 0 MID . ATL .

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

MID . ATL . 0. 0 3470. 0 0. 0 3471. 0

MID . ATL . 1. 0 1361. 0 0. 0 1361. 0

MID . ATL . 1. 0 1248. 0 0. 0 1249. 0 SO . ATL .

0. 0 16777. 0 3943. 0 20720. 0

SO . ATL . 0. 0 7069. 0 0. 0 7069. 0

SO . ATL . 0. 0 3013. 0 0. 0 3013. 0

SO . ATL . 0. 0 2838. 0 0. 0 2838. 0 MIDWES T

0. 0 19805. 0 0. 0 19806. 0

MIDHES T 0. 0 8779. 0 0. 0 6779. 0

MIDHES T 2. 0 2769. 0 0. 0 2771. 0

MIDHES T 2. 0 2540. 0 0. 0 2542. 0 SO . MES T

2. 0 41952. 0 0. 0 41954. 0

SO . WES T 5. 0 6037. 0 0. 0 6043. 0

SO . WES T 6. 0 3018. 0 0. 0 3024. 0

SO . NES T 6. 0 2768. 0 0. 0 2774. 0 CENTRA

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

CENTRA L 1. 0 698. 0 0. 0 899. 0

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

CENTRA L 2. 0 0. 0 0. 0 2. 0 NO . CNTRL

1. 0 3090. 0 2712. 0 5802. 0

NO . CNTRL 2. 0 0. 0 1352. 0 1354. 0

NO . CNTRL 3. 0 0. 0 0. 0 3. 0

NO . CNTRL 3. 0 0. 0 0. 0 3. 0 NES T

0. 0 6935. 0 0. 0 6935. 0

NES T 0. 0 3388. 0 0. 0 3388. 0

WES T 0. 0 1878. 0 0. 0 1878. 0

WES T 1. 0 1125. 0 0. 0 1126. 0 NO . WES T

0. 0 4855. 0 0. 0 4855. 0

NO . NES T 0. 0 2998. 0 0. 0 2998. 0

NO . WES T 0. 0 1280. 0 0. 0 1280. 0

NO . NES T 0. 0 1204. 0 0. 0 1204. 0 U S TOTA

L 3. 0 112679. 0 6655. 0 119337. 0

U S TOTA L 9. 0 36685. 0 1352. 0 38046. 0

U S TOTA L 14. 0 14227. 0 0. 0 14241. 0

U S TOTA L 15. 0 12355. 0 0. 0 12371. 0



# r



# C

## r 

# II

SIZ E CUSS : 150-20 0 TABLE 1 9 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

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



# c c c c BAS E CAS E NE N ENG . NAT . GAS 0. 0 RESIDOI L 1523. 0 COA L 0. 0 TOTA L 1523. 0
OPTIO N CAS E 1 NE N ENG . NAT . GAS 0. 0 RESI DOI L 828. 0 COA L 0. 0 TOTA L 828. 0
OPTIO N CAS E 2 NE N ENG . NAT . GAS 0. 0 RESI DOI L 362. 0 COA L 0. 0 TOTA L 362. 0
OPTIO N CAS E 3 NEHENG . NAT . GAS 0. 0 RESI DOI L 332. 0 COA L 0. 0 TOTA L 332. 0 N

N

N

N .Y./N.J . 0. 0 1625. 0 0. 0 1625. 0

.Y./N.J . 0. 0 1311. 0 0. 0 1311. 0

.Y./N.J . 0. 0 684. 0 0. 0 684. 0

.Y./N.J . 0. 0 627. 0 0. 0 627. 0 MIO . ATL .

0. 0 6207. 0 0. 0 6207. 0

MID . ATL . 0. 0 3769. 0 0. 0 3769. 0

MID . ATL . 0. 0 1650. 0 0. 0 1650. 0

MID . ATL . 0. 0 1513. 0 0. 0 1513. 0 SO . ATL .

0. 0 15149. 0 0. 0 15149. 0

SO . ATL . 0. 0 5887. 0 0. 0 5887. 0

SO . ATL . 0. 0 2575. 0 0. 0 2575. 0

SO . ATL . 0. 0 2362. 0 0. 0 2362. 0 MIDHES T

0. 0 15608. 0 0. 0 15608. 0

MIDHES T 0. 0 6697. 0 0. 0 6697. 0

MIDHES T 0. 0 2938. 0 0. 0 2938. 0

MIDHES T 0. 0 2694. 0 0. 0 2694. 0 SO . HES T

3. 0 33761. 0 0. 0 33764. 0

SO . HES T 5. 0 6699. 0 0. 0 6904. 0

SO . HES T 5. 0 3018. 0 0. 0 3023. 0

SO . HES T 5. 0 2768. 0 0. 0 2773. 0 CENTRA

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

CENTRA L 1. 0 920. 0 0. 0 921. 0

CENTRA L 1. 0 402. 0 0. 0 403. 0

CENTRA L 1. 0 369. 0 0. 0 370. 0 N

O

N O

N O

N O . CNTR

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

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

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

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

0. 0 4110. 0 0. 0 4110. 0

HES T 0. 0 2972. 0 0. 0 2972. 0

HES T 0. 0 1420. 0 0. 0 1420. 0

HES T 0. 0 1317. 0 0. 0 1317. 0 NO . HES T

0. 0 6394. 0 0. 0 6394. 0

NO . HES T 0. 0 3679. 0 0. 0 3679. 0

NO . HES T 0. 0 1610. 0 0. 0 1610. 0

NO . HES T 0. 0 1476. 0 0. 0 1476. 0 U S TOTA

L 4. 0 90918. 0 1196. 0 92117. 0

U S TOTA L 6. 0 32961. 0 546. 0 33515. 0

U S TOTA L 8. 0 14659. 0 0. 0 14667. 0

U S TOTA L 8. 0 13459. 0 0. 0 13467. 0



# c c c i c

# r

SIZ E CUSS : > 25 0 TABL E 2 1 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSm . I<»8*-199 0 S0 2 EMISSIONS (SHOR T TONS )



# c r c c BAS E CAS E NEHENG . NAT . GAS 0. 0 RESI DOI L 797. 0 COAL . 0. 0 TOTA L 797. 0
OPTIO N CAS E 1 NEHENG . NAT . 6AS 0. 0 RESI DOI L 797. 0 COA L 0. 0 TOTA L 797. 0
OPTIO N CAS E 2 NEHENG . NAT . 6A S 0. 0 RESI DOI L 349. 0 COA L 0. 0 TOTA L 349. 0
OPTIO N CAS E 3 NEHEH6 . NAT . GA S 0. 0 RESI DOI L 320. 0 COA L 0. 0 TOTA L 320. 0 N

N

N

N .Y./N.J . 0. 0 1949. 0 0. 0 1949. 0

.Y./N.J . 0. 0 1949. 0 0. 0 1949. 0

Y./N.J . 0. 0 947. 0 0. 0 947. 0

Y./N.J . 0. 0 668. 0 0. 0 668. 0 MID . ATL .

0. 0 3825. 0 3043. 0 6868. 0

MID . ATL . 0. 0 3825. 0 3043. 0 6868. 0

MID . ATL . 0. 0 2964. 0 0. 0 2964. 0

MID . ATL . 0. 0 2719. 0 0. 0 2719. 0 SO . ATL .

0. 0 10589. 0 0. 0 10589. 0

SO . ATL . 0. 0 10589. 0 0. 0 10589. 0

SO . ATL . 0. 0 4633. 0 0. 0 4633. 0

SO . ATL . 0. 0 4250. 0 0. 0 4250. 0 MIDHES T

0. 0 6140. 0 5071. 0 13211. 0

MIDHES T 0. 0 6140. 0 5071. 0 13211. 0

MIDHES T 0. 0 5431. 0 0. 0 5431. 0

MIDHES T 0. 0 4981. 0 0. 0 4981. 0 SO . HES T

3. 0 22605. 0 0. 0 22608. 0

SO . HES T 3. 0 22605. 0 0. 0 22608. 0

SO . HES T 3. 0 9890. 0 0. 0 9893. 0

SO . HES T 3. 0 9070. 0 0. 0 9073. 0 CENTRA

L 0. 0 512. 0 1893. 0 2406. 0

CENTRA L 0. 0 512. 0 1893. 0 2406. 0

CENTRA L 0. 0 922. 0 0. 0 922. 0

CENTRA L 0. 0 645. 0 0. 0 646. 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. 0 325. 0 326. 0

NO . CNTR

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

0. 0 4114. 0 0. 0 4114. 0

HES T 0. 0 4114. 0 0. 0 4114. 0

HES T 0. 0 2303. 0 0. 0 2303. 0

HES T 0. 0 2125. 0 0. 0 2125. 0 NO . HES T

0. 0 5294. 0 0. 0 5294. 0

NO . HES T 0. 0 5294. 0 0. 0 5294. 0

NO . HES T 0. 0 2317. 0 0. 0 2317. 0

NO . HES T 0. 0 2125. 0 0. 0 2125. 0 U S TOTA

L 5. 0 57826. 0 12036. 0 69867. 0

U S TOTA L 5. 0 57626. 0 12036. 0 69867. 0

U S TOTA L 5. 0 29755. 0 325. 0 30064. 0

U S TOTA L 5. 0 27303. 0 325. 0 27632. 0



### ( 

# c c c r o

### ( 

# r 

# r r c 

# c r

c c c SIZECUSS : 200-25 0

BAS E CAS E NE HENG . NAT . GA S 0. 0 RESI DOI L 266. 0 COAL 0. 0 TOTAL 266. 0
OPTION CAS E 1 NE HENG . NAT . GA S 0. 0 RESI DOI L 266. 0 COAL 0. 0 TOTAL 266. 0
OPTION CAS E 2 NE HENG . NAT . GA S 0. 0 RESI DOI L 155. 0 COAL 0. 0 TOTAL 155. 0
OPTION CAS E 3 NE HENG . NAT . GA S 0. 0 RESI DOI L 142. 0 COAL 0. 0 TOTAL 142. 0 TABL E 2 0 — INDUSTRIAL BOILERNSP S REGIONAL IMPACT S BYBOILERSIZE . 1986-199 0

30 2 EMISSION S (SHORT TONS )

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. 0 310. 0 0. 0 310. 0

.Y./N.J . 0. 0 285. 0 0. 0 285. 0 MID . ATL .

0. 0 4214. 0 0. 0 4214. 0

HID . ATL . 0. 0 2424. 0 0. 0 2424. 0

MID . ATL . 0. 0 1136. 0 0. 0 1138. 0

MID . ATL . 0. 0 1044. 0 0. 0 1044. 0 SO . ATL .

0. 0 8236. 0 0. 0 8236. 0

SO . ATL . 0. 0 3627. 0 0. 0 3627. 0

SO . ATL . 0. 0 1567. 0 0. 0 1587. 0

SO . ATL . 0. 0 1455. 0 0. 0 1455. 0 MIDHES T

0. 0 15052. 0 0. 0 15052. 0

MIDHES T 0. 0 4536. 0 0. 0 4536. 0

MIDHES T 0. 0 2001. 0 0. 0 2001. 0

MIDHES T 0. 0 1635. 0 0. 0 1835. 0 SO . HES T

0. 0 28729. 0 0. 0 28729. 0

SO . HES T 0. 0 10565. 0 0. 0 10565. 0

SO . HES T 4. 0 2449. 0 0. 0 2453. 0

SO . HES T 4. 0 2246. 0 0. 0 2250. 0 CENTRA

L 0. 0 3163. 0 0. 0 3163. 0

CENTRA L 0. 0 788. 0 0. 0 788. 0

CENTRA L 0. 0 190. 0 0. 0 190. 0

CENTRA L 0. 0 174. 0 0. 0 174. 0 NO . CNTR

L 0. 0 0. 0 2623. 0 2623. 0

NO . CNTR

L 0. 0 0. 0 1545. 0 1545. 0

NO . CNTR

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

NO . CNTR

L 1. 0 0. 0 0. 0 1. 0 HES T

0. 0 1141. 0 0. 0 1141. 0

HES T 0. 0 816. 0 0. 0 816. 0

HES T 0. 0 490. 0 0. 0 490. 0

HES T 0. 0 459. 0 0. 0 459. 0 NO . HES T

0. 0 1863. 0 0. 0 1863. 0

NO . HES T 0. 0 1064. 0 0. 0 1064. 0

NO . HES T 0. 0 466. 0 0. 0 466. 0

NO . HES T 0. 0 427. 0 0. 0 427. 0 U S TOTA

L 0. 0 63307. 0 2623. 0 65930. 0

U S TOTA L 0. 0 24729. 0 1545. 0 26273. 0

U S TOTA L 5. 0 8786. 0 0. 0 8791. 0

U S TOTA L 5. 0 8067. 0 0. 0 8072. 0



### (

# c r r r c c c r 

# I I

SIZ E CUSS : 100-15 0

BAS E CAS E TABL E 2 2 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE . 1986-199 0 FOSSI L FUE

L DEMAN D(10** 9 BTUS )

( 

# c c c NEHENG .

NAT . GAS 0. 0 RESI DOI L 2663. 0 COA L 0. 0 TOTA L 2683. 0

, OPTIO N CAS E 1 NEHENG . NAT . GAS 0. 0 RESI DOI L 2683. 0 COA L 0. 0 TOTA L 2683. 0
OPTIO N CAS E 2 NEHENG . NAT . GAS 0. 0 RESI DOI L 2663. 0 COA L 0. 0 TOTA L 2683. 0
OPTIO N CAS E 3 NEHENG . NAT . GAS 1369. 0 RESI DOI L 1314. 0 COA L 0. 0 TOTA L 2683. 0 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 . 548. 0 2628. 0 0. 0 3176. 0

.Y./N.J . 548. 0 2628. 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 . 2464. 0 7775. 0 0. 0 10238. 0

HID . ATL . 2464. 0 7775. 0 0. 0 10238. 0 SO . ATL .

0. 0 16261. 0 1424. 0 17664. 0

SO . ATL . 0. 0 17684. 0 0. 0 17684. 0

SO . ATL . 0. 0 17664. 0 0. 0 17664. 0

SO . ATL . 0. 0 17684. 0 0. 0 17684. 0 MIDHES T

821. 0 22119. 0 0. 0 22940. 0

MIDHES T 821. 0 22119. 0 0. 0 22940. 0

MIDHES T 7116. 0 15823. 0 0. 0 22940. 0

MIDHES T 7118. 0 15823. 0 0. 0 22940. 0 SO . HES T

5530. 0 32084. 0 0. 0 37613. 0

SO . HES T 17520. 0 20093. 0 0. 0 37613. 0

SO . HES T 20367. 0 17246. 0 0. 0 37613. 0

SO . HES T 20367. 0 17246. 0 0. 0 37613. 0 CENTRA

L 0. 0 6187. 0 0. 0 6187. 0

CENTRA L 3942. 0 2245. 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 2902. 0 3614. 0 2847. 0 9362. 0

NO . CNTR

L 6515. 0 0. 0 2847. 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

0. 0 11224. 0 0. 0 11224. 0

HES T 0. 0 11224. 0 0. 0 11224. 0

HES T 0. 0 11224. 0 0. 0 11224. 0

HES T 4106. 0 7118. 0 0. 0 11224. 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 . HES T 0. 0 7501. 0 0. 0 7501. 0 U S TOTA

L 10348. 0 113990. 0 4271. 0 128608. 0

U S TOTA L 29894. 0 95867. 0 2847. 0 128608. 0

U S TOTA L 46045. 0 62563. 0 0. 0 128608. 0

U S TOTA L 51520. 0 77088. 0 0. 0 128608. 0



# cSIZ E CUSS : 150-20 0 TABL E 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 ) 

# r c r r c c c BAS E CAS E NEHENG . NAT . GA S 0. 0 RESI DOI L 2070. 0 COA L 0. 0 TOTA L 2070. 0
OPTIO N CAS E 1 NEHENG . NAT . GAS 0. 0 RESI DOI L 2070. 0 COA L 0. 0 TOTA L 2070. 0
OPTIO N CAS E 2 NEHENG . NAT . GAS 0. 0 RESI DOI L 2070. 0 COA L 0. 0 TOTA L 2070. 0
OPTIO N CAS E 3 NEHENG . NAT . GAS 0. 0 RESI DOI L 2070. 0 COA L 0. 0 TOTA L 2070. 0 N

N

N

N .Y./N.J . 0. 0 3909. 0 0. 0 3909. 0

.Y./N.J . 0. 0 3909. 0 0. 0 3909. 0

.Y./N.J . 0. 0 3909. 0 0. 0 3909. 0

•Y./N.J . 0. 0 3909. 0 0. 0 3909. 0 MID . ATL .

0. 0 9811. 0 0. 0 9811. 0

HID . ATL . 0. 0 9811. 0 0. 0 9811. 0

MID . ATL . 383. 0 9428. 0 0. 0 9811. 0

MID . ATL . 383. 0 9428. 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 MIDHES T

0. 0 16766. 0 0. 0 16766. 0

MIDHES T 0. 0 16786. 0 0. 0 16786. 0

MIDHES T 0. 0 16786. 0 0. 0 16786. 0

MIDHES T 0. 0 16786. 0 0. 0 16766. 0 SO . HES T

6968. 0 26214. 0 0. 0 35182. 0

SO . HES T 17936. 0 17246. 0 0. 0 35182. 0

SO . HES T 17936. 0 17246. 0 0. 0 35182. 0

SO . HES T 17936. 0 17246. 0 0. 0 35182. 0 CENTRA

L 0. 0 5059. 0 0. 0 5059. 0

CENTRA L 2759. 0 2300. 0 0. 0 5059. 0

CENTRA L 2759. 0 2300. 0 0. 0 5059. 0

CENTRA L 2759. 0 2300. 0 0. 0 5059. 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 HES T

0. 0 8508. 0 0. 0 8508. 0

HES T 0. 0 8508. 0 0. 0 8508. 0

HES T 0. 0 8506. 0 0. 0 8508. 0

HES T 0. 0 8508. 0 0. 0 8508. 0 NO . HES T

0. 0 9198. 0 0. 0 9198. 0

NO . HES T 0. 0 9198. 0 0. 0 9198. 0

NO . HES T 0. 0 9198. 0 0. 0 9198. 0

NO . HES T 0. 0 9198. 0 0. 0 9198. 0 U S TOTA

L 12417. 0 97652. 0 1150. 0 111219. 0

U S TOTA L 25524. 0 84545. 0 1150. 0 111219. 0

U S TOTA L 27057. 0 84162. 0 0. 0 111219. 0

U S TOTA L 27057. 0 84162. 0 0. 0 111219. 0



# c c c c

# rI I £ 

# c c c r c c c

f



### ( 

# c 

# c c SIZ E CUSS : 200-25 0

BAS E NAT . 6AS RESI DOI L COA L TOTA L CAS E

NEHENG . 0. 0 887. 0 0. 0 887. 0
OPTIO N CAS E 1 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 887. 0 0. 0 887. 0
OPTIO N CAS E 2 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 887. 0 0. 0 887. 0
OPTIO N CAS E 3 NAT . GAS RESIDOI L COA L TOTA L NEHENG .

0. 0 887. 0 0. 0 887. 0 N

N

N

N TABL E

.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 2 4 —

INDUSTRIA

L BOILE R

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

• FOSSI L

. 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 NSP S REGIONA L IMPACT S B

YBOILE R FUE L DEMAN D

HIDHES 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 (10** 9 BTUS )

SO . HES T 0. 0 26411. 0 0. 0 26411. 0

SO . HES T 0. 0 26411. 0 0. 0 26411. 0

SO . HES T 12417. 0 13994. 0 0. 0 26411. 0

SO . HES T 12417. 0 13994. 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 887. 0 1084. 0 0. 0 1971. 0

CENTRA L 687. 0 1084. 6 0. 0 1971. 0 SIZE , 1986 -

NO . CNTR

L 0. 0 0. 0 3252. 0 3252. 0

NO . CNTR

L 0. 0 0. 0 3252. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0

NO . CNTR

L 3252. 0 0. 0 0. 0 3252. 0 199 0

HES T 0. 0 3055. 0 0. 0 3055. 0

HES T 0. 0 3055. 0 0. 0 3055. 0

HES T 0. 0 3055. 0 0. 0 3055. 0

HES T 0. 0 3055. 0 0. 0 3055. 0 NO . HES 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 0. 0 2661. 0

NO . HES T 0. 0 2661. 0 0. 0 2661. 0 U S TOTA

L 0. 0 63762. 0 3252. 0 67014. 0

U S TOTA L 0. 0 63762. 0 3252. 0 67014. 0

U S TOTA L 16556. 0 50458. 0 0. 0 67014. 0

U S TOTA L 16556. 0 50458. 0 0. 0 67014. 0



# c c

# c r c r

C C 

# c c c SIZ E CUSS : > 25 0

BAS E CAS E NEHEN6 . NAT . 6A S 0. 0 RESI DOI L 1993. 0 COA L 0. 0 TOTA L 1993. 0
OPTIO N CAS E 1 NE HENG . NAT . GAS 0. 0 RESI DOI L 1993. 0 COA L 0. 0 TOTA L 1993. 0
OPTIO N CAS E 2 NEHEN6 . NAT . GAS 0. 0 RESI DOI L 1993. 0 COA L 0. 0 TOTA L 1993. 0
OPTIO N CAS E 3 NEHENG . NAT . GAS 0. 0 RESI DOI L 1993. 0 COA L 0. 0 TOTA L 1993. 0 TABL E 2 5 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0 FOSSI L FUE

L DEMAN D(10** 9 BTUS )

N

N

N

N .Y./N.J . 0. 0 5409. 0 0. 0 5409. 0

.Y./N.J . 0. 0 5409. 0 0. 0 5409. 0

.Y./N.J . 0. 0 5409. 0 0. 0 5409. 0

.Y./N.J . 0. 0 5409. 0 0. 0 5409. 0 MID . ATL .

0. 0 10534. 0 6406. 0 16940. 0

MID . ATL . 0. 0 10534. 0 6406. 0 16940. 0

MID . ATL . 0. 0 16940. 0 0. 0 16940. 0

MID . ATL . 0. 0 16940. 0 0. 0 16940. 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 MIDHES T

0. 0 20356. 0 10676. 0 31032. 0

MIDHES T 0. 0 20356. 0 10676. 0 31032. 0

MIDHES T 0. 0 31032. 0 0. 0 31032. 0

MIDHES T 0. 0 31032. 0 0. 0 31032. 0 SO . HES T

9253. 0 56513. 0 0. 0 65766. 0

SO . HES T 9253. 0 56513. 0 0. 0 65766. 0

SO . HES T 9253. 0 56513. 0 0. 0 65766. 0

SO . HES T 9253. 0 56513. 0 0. 0 65766. 0 CENTRA

L 1424. 0 1281. 0 3986. 0 6690. 0

CENTRA L 1424. 0 1281. 0 3986. 0 6690. 0

CENTRA L 1424. 0 5267. 0 0. 0 6690. 0

CENTRA L 1424. 0 5267. 0 0. 0 6690. 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 HES T

0. 0 13523. 0 0. 0 13523. 0

HES T 0. 0 13523. 0 0. 0 13523. 0

HES T 0. 0 13523. 0 0. 0 13523. 0

HES T 0. 0 13523. 0 0. 0 13523. 0 NO . HES T

0. 0 13239. 0 0. 0 13239. 0

NO . HES T 0. 0 13239. 0 0. 0 13239. 0

NO . HES T 0. 0 13239. 0 0. 0 13239. 0

NO . HES T 0. 0 13239. 0 0. 0 13239. 0 U S TOTA

L 16655. 0 149325. 0 25338. 0 191316. 0

U S TOTA L 16655. 0 149325. 0 25338. 0 191318. 0

U S TOTA L 16655. 0 170393. 0 4271. 0 191318. 0

U S TOTA L 16655. 0 170393. 0 4271. 0 191318. 0



# c c c

# r r c r 

# I I

r r r SIZECUSS : 100-15 0

BAS E CAS E TABL E 2 6 — INDUSTRIAL BOILERNSP S REGIONAL IMPACT S B YBOILE RSIZE . 1966-199 0 ANNUALIZE DCOST S (10** 6 198 3 9 1

NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 22. 8 0. 0 22. 8
OPTIO N CAS E 1 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 23. 0 0. 0 23. 0
OPTIO N CAS E 2 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 23. 4 0. 0 23. 4
OPTIO N CAS E 3 NAT . GAS RESIDOI L COA L TOTA L NE

HENG . 13. 1 10. 2 0. 0 23. 4 N

N

N

N Y

Y

Y

.Y ./N.J . 0. 0 24. 8 0. 0 24. 8

./N.J . 0. 0 25. 3 0. 0 25. 3

./N.J . 5. 2 20. 4 0. 0 25. 7

./N.J . 5. 2 20. 5 0. 0 25. 7 MI D

MI D

MI D

MI D . ATL . 10. 4 69. 6 0. 0 79. 9

. ATL . 10. 4 72. 4 0. 0 62. 7

. ATL . 23. 3 60. 5 0. 0 63. 9

. ATL . 23. 3 60. 6 0. 0 83. 9 SO . ATL .

0. 0 126. 4 10. 7 137. 1

SO . ATL . 0. 0 144. 0 0. 0 144. 0

SO . ATL . 0. 0 147. 6 0. 0 147. 6

SO . ATL . 0. 0 148. 5 0. 0 148. 5 MIOHES T

7. 9 176. 2 0. 0 164. 1

MIDHES T 7. 9 163. 4 0. 0 191. 3

MIDHES T 68. 5 125. 9 0. 0 194. 4

MIDHES T 68. 5 125. 9 0. 0 194. 4 SO . HES T

44. 5 230. 8 0. 0 275. 3

SO . HES T 140. 2 151. 1 0. 0 291. 3

SO . HES T 161. 5 130. 6 0. 0 292. 1

SO . HES T 161. 5 130. 7 0. 0 292. 2 CENTRA

L 0. 0 47. 9 0. 0 47. 9

CENTRA L 34. 1 17. 2 0. 0 51. 4

CENTRA L 51. 1 0. 0 0. 0 51. 1

CENTRA L 51. 1 0. 0 0. 0 51. 1 NO .

NO .

NO .

NO . CNTR

L 23. 6 28. 5 18. 4 70. 5

CNTR L 52. 0 0. 0 18. 7 70. 6

CNTR L 71. 8 0. 0 0. 0 71. 8

CNTR L 71. 8 0. 0 0. 0 71. 8 HES T

0. 0 88. 3 0. 0 88. 3

HES T 0. 0 89. 6 0. 0 89. 6

HES T 0. 0 90. 5 0. 0 90. 5

HES T 37. 6 52. 8 0. 0 90. 3 

### NO .

NO .

NO .

NO . HES T 0. 0 57. 5 0. 0 57. 5

HES T 0. 0 57. 9 0. 0 57. 9

HES T 0. 0 59. 3 0. 0 59. 3

HES T 0. 0 59. 7 0. 0 59. 7 U S TOTA

L 86. 4 872. 8 29. 1 988. 3

U S TOTA L 244. 5 763. 6 18. 7 1027. 0

U S TOTA L 381. 4 658. 2 0. 0 1039. 6

U S TOTA L 432. 0 608. 9 0. 0 1040. 9


# c c rSIZ E CUSS : 150-20 0 TABL E 2 7 — INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0 ANNUALIZE

DCOST S (10** 6 196 5 9 ) 

# f BAS E CAS E



# r r r NAT . GAS

RESI DOI L COA L TOTA L NEHENG .

0. 0 15. 6 0. 0 15. 6
OPTIO N CAS E 1 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 16. 0 0. 0 16. 0
OPTIO N CAS E 2 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 16. 1 0. 0 16. 1
OPTIO N CAS E 3 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 16. 1 0. 0 16. 1 N

N

N .

N . .Y./N.J . 0. 0 29. 5 0. 0 29. 5

Y./N.J . 0. 0 29. 8 0. 0 29. 8

Y./N.J . 0. 0 29. 9 0. 0 29. 9

Y./N.J . 0. 0 30. 0 0. 0 30. 0 MI D

MID

MI D

MID . ATL . 0. 0 72. 4 0. 0 72. 4

. ATL . 0. 0 74. 3 0. 0 74. 3

. ATL . 3. 5 71. 4 0. 0 74. 9

. ATL . 3. 5 71. 4 0. 0 74. 9 SO . ATL .

0. 0 105. 6 0. 0 105. 6

SO . ATL . 0. 0 111. 1 0. 0 111. 1

SO . ATL . 0. 0 112. 0 0. 0 112. 0

SO . ATL . 0. 0 112. 0 0. 0 112. 0 MIDHES T

0. 0 123. 6 0. 0 123. 8

MIDHES T 0. 0 129. 9 0. 0 129. 9

MIDHES T 0. 0 130. 9 0. 0 130. 9

MIDHES T 0. 0 131. 0 0. 0 131. 0 SO . HES T

67. 9 181. 1 0. 0 249. 0

SO . HES T 135. 6 125. 5 0. 0 261. 3

SO . HES T 135. 8 126. 6 0. 0 262. 3

SO . HES T 135. 6 126. 6 0. 0 262. 4 CENTRA

L 0. 0 36. 3 0. 0 36. 3

CENTRA L 21. 0 17. 0 0. 0 38. 0

CENTRA L 21. 0 17. 2 0. 0 38. 2

CENTRA L 21. 0 17. 2 0. 0 38. 2 NO .

NO .

NO .

NO . CNTR

L 24. 2 9. 7 7. 5 41. 5

CNTR L 33. 9 0. 0 7. 6 41. 6

CNTR L 41. 7 0. 0 0. 0 41. 7

CNTR L 41. 7 0. 0 0. 0 41. 7 HES T

0. 0 60. 8 0. 0 60. 8

HES T 0. 0 61. 1 0. 0 61. 1

HES T 0. 0 61. 5 0. 0 61. 5

HES T 0. 0 61. 5 0. 0 61. 5 N

O

N O

N O

N O . HES T 0. 0 63. 5 0. 0 63. 5

. HES T 0. 0 64. 2 0. 0 64. 2

. HES T 0. 0 64. 6 0. 0 64. 6

. HES T 0. 0 64. 8 0. 0 64. 8 U S TOTA

L 92. 1 698. 2 7. 5 797. 8

U S TOTA L 190. 7 628. 9 7. 6 827. 2

U S TOTA L 202. 0 630. 3 0. 0 632. 3

U S TOTA L 202. 0 630. 6 0. 0 832. 6



# o c

# rl l
c c r TABL E 2 8

SIZ E CUSS : 200-25 0



# r c c r BAS E

NAT . 6AS RESI DOI L COA L TOTA L CAS E

NEHENG . 0. 0 6. 9 0. 0 6. 9
OPTIO N CAS E 1 NAT . GAS RESI DOI L COA L TOTA L NEHEN6 .

0. 0 6. 9 0. 0 6. 9
OPTIO N CAS E 2 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 7. 0 0. 0 7. 0
OPTIO N CAS E 3 NAT . GAS RESI DOI L COA L TOTA L NEHENG .

0. 0 7. 0 0. 0 7. 0 N

N

N

N Y

Y

Y

Y ./N.J . 0. 0 13. 8 0. 0 13. 8

./N.J . 0. 0 13. 8 0. 0 13. 8

./N.J . 0. 0 13. 9 0. 0 13. 9

./N.J . 0. 0 13. 9 0. 0 13. 9 MID . ATL

0. 0 48. 5 0. 0 48. 5

MID . ATL 0. 0 49. 5 0. 0 49. 5

MID . ATL 0. 0 49. 8 0. 0 49. 8

HID . ATL 0. 0 49. 9 0. 0 49. 9 INDUSTRIA

L BOILE RNSP S REGIONA

L IMPACT S B

YBOILE RSIZE , 1986-199 0 ANNUALIZE

DCOST S (10** 6 198 5 9 )



### SO .

SO .

SO .

SO . ATL . 0. 0 66. 4 0. 0 66. 4

ATL . 0. 0 68. 6 0. 0 68. 6

ATL . 0. 0 69. 2 0. 0 69. 2

ATL . 0. 0 69. 2 0. 0 69. 2 MIDHES T

0. 0 62. 2 0. 0 62. 2

MIDHES T 0. 0 68. 4 0. 0 88. 4

MIDHES T 0. 0 89. 1 0. 0 69. 1

MIDHES T 0. 0 69. 1 0. 0 89. 1 SO . HES T

0. 0 190. 4 0. 0 190. 4

SO . HES T 0. 0 200. 1 0. 0 200. 1

SO . HES T 95. 5 104. 6 0. 0 200. 0

SO . HES T 95. 5 104. 6 0. 0 200. 1 CENTRA

L 0. 0 14. 1 0. 0 14. 1

CENTRA L 0. 0 15. 4 0. 0 15. 4

CENTRA L 6. 9 8. 5 0. 0 15. 4

CENTRA L 6. 9 8. 5 0. 0 15. 4 NO .

NO .

NO .

NO . CNTR

L 0. 0 0. 0 23. 6 23. 6

CNTR L 0. 0 0. 0 23. 7 23. 7

CNTR L 23. 1 0. 0 0. 0 23. 1

CNTR L 23. 1 0. 0 0. 0 23. 1 HES T

0. 0 22. 2 0. 0 22. 2

HES T 0. 0 22. 3 0. 0 22. 3

HES T 0. 0 22. 4 0. 0 22. 4

HES T 0. 0 22. 4 0. 0 22. 4 

### NO .

NO .



### NO .

NO . HES T 0. 0 19. 2 0. 0 19. 2

HES T 0. 0 19. 4 0. 0 19. 4

HES T 0. 0 19. 6 0. 0 19. 6

HES T 0. 0 19. 6 0. 0 19. 6 U S TOTA

L 0. 0 463. 7 23. 6 487. 3

U S TOTA L 0. 0 484. 6 23. 7 508. 3

U S TOTA L 125. 5 364. 0 0. 0 509. 5

U S TOTA L 125. 5 384. 2 0. 0 509. 7 

# c c

t •

# r 

# I I

SIZ E CUSS : > 25 0 

# r 

# r r r

C 

# c c r TABL E 2 9 — INDUSTRIAL BOILERNSP S REGIONAL IMPACT S BYBOILERSIZE . 1986-199 0

ANNUALIZE D COST S (10»* 6 19S 5 9 )
BAS E NAT . 6AS RESI DOI L COA L TOTA L CAS E

NEHENG . 0. 0 15. 8 0. 0 15. 6
OPTIO N CAS E 1 NAT . GAS RESIDOI L COA L TOTA L NEHENG .

0. 0 15. 8 0. 0 15. 8
OPTIO N CAS E 2 NAT . GAS RESIDOI L COA L TOTA L NEHENS .

0. 0 16. 0 0. 0 16. 0
OPTIO N CAS E 3 NAT . 6AS RESI DOI L COA L TOTA L NEHENG .

0. 0 16. 1 0. 0 16. 1 N

N Y./N.J . 0. 0 41. 0 0. 0 41. 0

Y./N.J . 0. 0 41. 0 0. 0 41. 0

N.Y./N.J .

N 0. 0 41. 5 0. 0 41. 5

Y./N.J . 0. 0 41. 5 0. 0 41. 5 MID . ATL .

0. 0 60. 0 46. 0 126. 0

MID . ATL . 0. 0 60. 0 46. 0 126. 0

MID . ATL . 0. 0 127. 0 0. 0 127. 0

MID . ATL . 0. 0 127. 0 0. 0 127. 0 SO . ATL .

0. 0 197. 2 0. 0 197. 2

SO . ATL . 0. 0 197. 2 0. 0 197. 2

SO . ATL . 0. 0 199. 5 0. 0 199. 5

SO . ATL . 0. 0 199. 6 0. 0 199. 6 MIDHES T

0. 0 159. 4 76. 5 237. 9

MIDHES T 0. 0 159. 4 76. 5 237. 9

MIDHES T 0. 0 240. 4 0. 0 240. 4

MIDHES T 0. 0 240. 5 0. 0 240. 5 SO . HES T

79. 2 406. 5 0. 0 487. 7

SO . HES T 79. 2 406. 5 0. 0 467. 7

SO . HES T 79. 2 411. 9 0. 0 491. 1

SO . HES T 79. 2 412. 1 0. 0 491. 3 CENTRA

L 12. 2 9. 8 26. 0 50. 0

CENTRA L 12. 2 9. 8 28. 0 50. 0

CENTRA L 12. 2 39. 1 0. 0 51. 4

CENTRA L 12. 2 39. 1 0. 0 51. 4 NO .

NO .

NO .

NO . 

### _, CNTR

L 43. 8 0. 0 23. 9 67. 7

CNTR L 43. 8 0. 0 23. 9 67. 7

CNTR L 43. 8 0. 0 26. 9 70. 7

CNTR L 43. 8 0. 0 26. 9 70. 7 HES T

0. 0 98. 2 0. 0 98. 2

HES T 0. 0 98. 2 0. 0 98. 2

HES T 0. 0 98. 7 0. 0 98. 7

HES T 0. 0 98. 8 0. 0 98. 8 

### HO .

NO .

NO .



### NO . HES T 0. 0 95. 9 0. 0 95. 9

HES T 0. 0 95. 9 0. 0 95. 9

HES T 0. 0 97. 0 0. 0 97. 0

HES T 0. 0 97. 0 0. 0 97. 0 U S TOTA

L 135. 2 1105. 6 176. 5 1417. 6

U S TOTA L 135. 2 1105. 8 176. 5 1417. 6

U S TOTA L 135. 2 1271. 1 26. 9 1433. 2

U S TOTA L 135. 2 1271. 7 26. 9 1433. 9



# c . 

# c o c