CORPORATION
 ENERGY PENALTIES ASSOCIATED
WITH ENVIRONMENTAL REGULATIONS
   IN PETROLEUM REFINING
   VOLUME II:  APPENDICES

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CORPORATION
    DCN  78-100-134-02-04
    EPA  Project No.  68-02-4128-2
                         ENERGY PENALTIES ASSOCIATED

                        WITH ENVIRONMENTAL REGULATIONS

                            IN PETROLEUM REFINING
                           VOLUME II:  APPENDICES
                                  April  1978
                              Presented  to:

                     ENVIRONMENTAL PROTECTION AGENCY
                            Washington,  D.C.
                     EPA Project Officer:  Bob  Fuhrman
                               Prepared by:

                               J. D. Colley
                               G. E. Harris
                              W. R. Phillips
                             W. C. Micheletti
            8500 Shoal Creek Blvd./P.O. Box 9948/Austin, Texas 78766/(512)454-4797

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                 TABLE OF CONTENTS (Cont'd.)
                           Volume II


APPENDIX A   Environmental Regulations by Pollutant

APPENDIX B   Study Results - Forms 1 Through 6

APPENDIX C   United States Refineries by Companies
                              11

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            APPENDIX A
Environmental Regulations by Pollutant

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                                                               TAIH.E A-I.   ArTUCAUl.K I'ARTlCULA'rt: KECUI.ATIONS
                        AIJCII  1
                                                    CoiuhuBllmi  Un
                                                                                                                                             Catalytic Cracking  Unltu
>
N)
                                  EXIST INI;

                         CLASS 1 COUNTIES

Alabama      2,4.5       For  units <10x10° Utu/hr
                         E  =  0.5
                         For  units >IO»IO' Uiu/hr
                         und  <250xlo'_htu/hr
                         E' *  1.3B (II)  ••''''
                         For  units >250xiu' Utu/hr
                        : E  -  0.12
                         Where:
                         E  -  eiuUtilons (Ib/IO' Utu)
                         II  -  heat Input (I0' Utu/hr)

                         CLASS 2 COUNTIES

                         For  unltu -10x1(1* Uiu/hr
                         E  -  O.H
                         For  milts >IOxlo' Utu/hr
                         and  <250xlO(  Utu/hr
                         E  =•  3. 10'J 25Uxlo' Utu/hr
                         E  -  0.12
                                                                         NEW
                                                                   Subject  lu Hit:
                                                                   rult:s  uud rugu-
                                                                   liiilouii  t'ur
                                                                   CUSS  1  COUNTIES
                                                                   rcgurdluuti of
                                                                   their  local Ian.
CLASS I COIINT1ES

For units  <3»  tons/hr
E •- 3.5'J  (f)"'42
For unltu  >30  tons/hr
E - 17.31  (P)" "
Where:
E * emissions  (Ib/lir)
H =* process weight
    (toiis/hr)
                      CUSS 2 COUNTIES

                      For uulta <30 ton
                      E = 4.10 (»•)*'"
                      For uitltu >'JO toi
                      E - (55.0 (I-)"' "
                                                   Subject til the
                                                   rules imJ regu-
                                                   laf louu (or
                                                   CUSS 1 COUNTIES
                                                   regurJIesu ot'
                                                   tlielr location.
                                                                                                                                           Same as I'rocess      Saiuu  as
                        U.'J         o. 10 gruluu/SCF
                                    (Exchiulng wood uuatu
                                    unItu)
0.05 graluu/SCF
(Ejtcludliig coul
or launlclpul
uuule coubuutIon
units)
                                                                             0.40  gruln/SCf
                             0.05 grain/set'
0.10 gralu/SCF
                                                                                                                                                     0.05  grain
                                                                                                                                                           /SCF
           Arizona
                         For  mills <4.2»10" Ulu/hr
                         E  =  1.02 (<))"•"'
              15        J  For  milts >4.2xlO* Utn/hr
                         E  -  17.0 (Q)"-'-"
                         Where:
                         E  -  emissions (Ib/hr)
                       -I)  -  heat  Input (III' Dlu/hr)
                                                                       eklatlllg
                                                                                        None                         Noau
                      For nnltu <10 ton/lir
                      E - 3.59 (H)0'"
                      For Unllu >"ll) fon/lir         ..
                      E - 17 31 (I')0'"'                eklutlng
                      Uhere:
                      E =* euuitltiulonu (Ib/lir)
                      P * process weight  (ton/hr)
                                                                                                                                           STATE
                                                                                                                                           <0.17 Ib/io'll)
                                                                                                                                           gati corrected
                                                                                                                                           to 121 COj
                                                                                              See Exist I U

-------
           TAIil.K A-l  (Continued)
Slate AIJCK f Combustion Units
EXISTING NEU
Arkansas IH <75 lig/M1 for a 24 lir For A < 1.00(1
period E - O.W54 (A)"'""
<1SO MB/V for u lU-uhi For A> t.OOO
a«B- E - 0.977 (A)"'"
Where:
A » potential
emission without
control (Ib/hr)
E = allowable
ewlualuii (Ib/hr)
Process UultB Catalytic (bracking
EX 1ST INC NEW EX 1ST INC NKW
For 1' < 10 Ions/in See Eilsl lug None None
E - 1.5H (P)°'"
For P>10 toiis/hr
E - 17.11 (P)°'u
Wlie ic :
I1 * iiruucmi ucl gltt
(luitti/ltr)
E a allowable uiultiuluii
(Ib/hr)
Note; £ caiutui uxtiueU
                                                                                            1000  Ib/day or  100 Ib/hr
            Call lorn I a
                                      -'0.1
                                                                   <10 Ik/In
U)
                                      <0.15 graln/Jiy
                                      SCF exhaust gau vuluiue
                                      For unllu >250xlO( tttu/
                                      hr.
                                      E < 0.10 lb/10' htu
                                      heat Input
                                                                                           Sue Comliout ion  UnlCti
For P500
E - 10
Where:
P " proceuu weight

E - uuiljjlou rate
    (Ib/br)

For l'<10
E - 4.1 (I-)0'"
For P > 10
E •• 40"Ib/hr or
O.I grain/ft'
                                                                                                                                                             iicc  l'roct:utt

-------
TAUI.E  A-l
    Slult:       AfjCK t
California       31
                                             Combust Ion Unllti
                                     KX IS II HI.
                                     HliM

                                ujonu  (Ib/ltr)
                                                                                                               I1 - i*rocetio  ratti
                                                                                                                                                               MM
E - 4.1  (I')"'1''          Sue frocoua      Sue I'luceja
Where:                    Unltu            Unllu
E - i.-iuUulonti (Ib/lir)

    (tuna  Input/Ill)
Note: E  nunnot exceed
40 ll>/lu or 0.1 grain/
ft*
                                                                                                                            Sou I'r
                                                                                                                            Hulls
                                                                                                               Note ; li cannot
Colorado       35.36
Fur VI <  1.0.  U - U.5
Kor 1.  500
K - 0.1
Ulicre:
Kl - luel  Input (III'
     litu/lu')
K ° alluwablu  eulusluii
    (Ib/IU6  Uiu)
                                                              Suu tulullni;
                                                                                     Fur 1'  <  JU
                                                                                     t = 3.59  (P)"'"
                                                                                     For f  >  30
                                                                                     li » 1/731  (I-)"'"
                                                                                     Where:
                                                                                     1* = prucucju uul^lti
                                                                                         (l»l>/lu)
                                                                                     H = ullouablu uuiluti
                                                                                         (Ib/lir)
       l ui 1 ng
                          lli.Ua
                                           tiet I'l
                                           Unltu
                              <0.20 lb/10k  Bl"
                              heat Input
                                <0.10 lb/10*  Btu
                                heac Input
For F <  30               Suu Kulsilli
E - 3.5"  (I-)""2
For I' >  30
E = I?T3I  (I')"'"
                          Suu frocusu      Si:t: l'i
                          Uuilu            Hi. i Hi
                                                                                          (con/In-)
                                                                                     li =  allikuiiblc uul mi ton
                                                                                          (Ib/lir)

-------
          TAUI.E  A-l   (CunLinuutl)
 I
Oi
Stale A(;CK 1

ware 45 See
Ida • 5 Sue
fcla 2. 4'J. Fur
59. 5B P =
Fur
and
Cuuibus t lun Units
EX 1ST INC NEW
Peimay 1 vanl a
MliiHiaalppl
units IO' Utu/hr Fur oiiliu >\u' Utu/hr
<2»IO" 111. ,/l,i and <250«10' Ucu/ln
Pruceaa Units
EX^STINC Nia;
'

E - 4. t (P)"'" Fur P < 3O
E = alluuable eiula- £ " 4.1 (P)"'"
a lun Ob/br) Fur P > JO
P » prui:eati weight E =• |55 (P)°"")-40
('tilal yl 1 4: 1'racklng
EiiisTiNi; NI:M


See Prucetiti See Prufeiis
Unlla Unllu
          Hawaii
                              1,0
                                                                   - 0.5(10)B-5/H
                                     Fur onllii >2nl09 Utu/hr     Fur unlla >250xlOl> Ulu/br
                                     P = 0.24                    P  =• 0. 10
                                     Ulm re:
                                     P ~ alluwable weight
                                     (lb/10' Ulu beat Input)
                                     K - Heat Input  (Ifl' 111,,/
                                     I,.)
                                     <0.4 lb/100 Ib
                                     uf bagaiibe— at* bui'ned
                              for P JO
                              E - 40.0
                              Uhure:
                              E = allowable euilii-
                                  alou (Ib/ln)
                              P = process weight
                                  (I out./In )
                                                     Same  as  Existing
                                               See Pruueas
                                               Unltu
Sue Prucesi*
Hulls
                                     Fur units < 10' Utu/br
                                     E = 0.6
                                     Fur units > IOV Ulu/br
                                     and < 10'" Ulu/br
                                     E - 102.59 (II)1"2'
                                     Fur units > 10'" Btu/br
                                     E - 0.12
                                     Where;
                                     E a alluwable eiulssluna
                                         (II,/IOC Ulu)
                                     II = heal Input (I01* Ulu)
  JO
E = 55.0  (P)"' "
Where:

    (lun/br)
E ~ allowable  emlu-
    sluns (Ib/hr)

-------
TAUI.E A-l   (Continued)
InJiauu
ACJCIi 1 Cuulmstlun Units
EJISTIMij NEW
a 70. 74 0.10 Ib/iu' Utu of Set: Enisling
actoal licat Input lor
liquid and combination
llt|uld and gaseous
fuels. No regulation
" V





67. HO For Qw < 1O P - ifi;f(o~T'>V75V~Yl)'rrir
P < 0.6 P not to exceed 0.6 for
Fur 10 < Qni < 10s mi 1 in <250»10' Utu/hr
P - O.B7(Qui) •'" 0.6 for unltu <250*10k
Fur Qia > IO*1 Utu/lir
Where: fur unltu > 250xlu'
CJili " total (ilant Utu/hr
uuuratlnt; capacity Where:
rating (10 btu/lir) n ^ nuiulier of utacktj In
P - Ib part Iculate/ fuel burning operation
I0l Ulu a - 0.67 (pluiu: rUe
Process Uullu
EXIS'I'IHU HEW
For P < 10 For P < 450
E = 4.10  10 For t > 450
t - 55.0(P)"' "-40 E * 24TB(I')°'"
Where:
ulon (Ib/br)
P ^ procctiu weight
(ton/In)



For P < 10 iiaiue au Existing
E - 4.10 (P)°'*v
For P > 10
E - |55.0(l')"' "1-40
Where:
slon (lb/l.r)
P s process weight
(toil/Ill)



('atalytlc Cracking
EXISTING NEW
For P •• 10 See Exist li
E - 4.10 (P)0'"
For f > 10
E - S5.0(P)"- "-40
Uheie:
uion (Ib/lu)
P = catalyst reclr-
culatlon rate. In-
cluding amount ot ~~
fresli catalyst added
(tun/In)
O.OU of 1 he re- Same as
cala lyjt








                                                 facioi)

                                                 Ita - titack  he I Kin In ft.
                             ('auix  a ha
                         r = ir$'~(^°
                         Variable^ itt* U
a a Above
                                                       Same ay
                                                       Above

-------
             TAIH.L A-1   (ConL timed)
>
 I
ale AIJCK I Cuuliuntlun Hulls
EXISTINti NI.U
i 65 Fur uullu >250x)01' See Existing
Ulu/hr
E '• 0. 10 lb/10' Ulu




as 94,46-100 Fur I) < 10 Sec Existing
E - 0.6(1
Fur 10 < 0 < 10s
E - I.026(Q) *' 2> J
Fur Q > 10H
E - 0.12
Where:
 10* Fur (J > 250
E = 0.11 E = 0.10

I'rlurl ly 11 Mellon
Fur (| < 10~
E = 0.75
Fur 10 < l| < 10*
E = 1.2b25(i|)~''21J
Fur Q > 1011
E * 0.15
Prior 1 t.y_n L "eijlui"
Fur (( < 10
E - 0.80
Fur 10 < () < ]0\
E '•* l.JI52(0) ' " ' * a "*
Fur fj > 10*
E - 0.1U
Where:
I) - heal li,|H,l
(IO' Uiu/hr)
E - allowable ciuluiiluii
(Ib/I0e Dili)

EX 1ST INC NEW
Fur 1' < '10 See Existing
E = 4.10(1')"'"
Fur 1' > 'ill
E - (55. 0(1')"' ' ' |-40
"''•'piuces. weight
E - allulih'L eiula-
1,1 on (Ib/hr)
Fur V < 10 See Exlutlng
E •» 4.10(1')""'''
Fur 1' > iO
E = |55.0(F)"' "|-40
Where:
I' - process weight
(ion:, /In)
E E allowable eiulu-
Sluil ( Ill/I, l)



For F < 10 For F < iO
E = 4.1O(P)°'" . E = 3.59(F)°"'Z
For F > :(0 Fur 1' > 10
E =• |55.0(l')°' " )-40 E •= 17.11(F)°' "
Uhe re :
I* = prucess weight
(tons/hr)
E - ulluwahle eluU-
blun (Ib/hr)
ur
0.02 grulus/SCF of
exit gas vu 1 uuie
ur
972 recovery efficiency












Catalytic Cracking Uiillu
SSlsiUfi: »™
t < i.U Ib/IUMh ^.:e t-KUtliit;
ui i:uku tin nut tf
la rc^eiieranji




See I'ruceas See 1'rucess
Units Hulls










Same as Prucess 1.0 Ib/IO'lh
Uulls of 4:oke buru-
uff In the
' catatysl re-
geueratur
(an ailJI l ioii-
al 0. 10 Ib/
IOL Uln uf
heal litpui
If wasle
heal bul ler
Is use.!)















-------
TAUI.KA-l   (Conciuued)
Stale AIJCK 1

Coiuiniatlon Units I'roceus Unllu Catalytic Cracking llnlls
EXISTS: NEW ES!.5'tlffii NEW MiS.'!'.UK; NEW
1 on i s 1 'ii iti 1U6 *- 0
huat





Hu 1 in: 1 09 for
For
E -

lii|Jui: t - 'i . 10(P) * ' ** 7 Uiiiia





For P > 30
Ubiiri"'001*""1"*0
(lon/br)
E e allowable emission '
(Ib/br)
10.B2(<()"0'"' E - 3.5a(f)°'t:' Iliilta
Q > 150 For 1' > 30
3.0 E » l/.31(l-)°-"
Where: Uhere: A
(j =
I^*
1 E -
oo k
Maryland 115.116 Fur
E -
Fur
E -
Ube i
Q »
beat
(10*
1 1
li)|>uf H = (irocuss weight
Utu/hr) (lun/hr)
ill i.' i i i i i i
sion (lb/10' Utu) (Ih/lu)
Q <
0.6
Q >
0.12
•e :
heat
10"

10"


Input (lu1
l>l,,/lll)
E -
Ullll
wable eiulsuloii
(lb/106 Utu)

-------
TAULK  A-l   (Continued)
AljCU 0 Combustion
EXISTING
42 E < 0. 12
119 E < 0.15
Where:
1) = heat Inunt Uo'Utu}
Units Process Units
MEW EXISTING
"For 3 < (| < 250 E - %( | 55.0(P) * ' " |-40)
E = 0.10 ,
For Q > 250 E - | 55. 0(P) ' ' " |-40
E - 0.05
Catalytic Cracking Units
NEW EXISTING NEW
E - ^1(55.0 Same as Process Same as Pro-
(P)° "|-40| Units cess Units
                             E = allowable  euluslous
                                      U&  Utu)
                       122   For S <  100
                             E - 0.65
                             For 100  < S  <  300
                             0.45 < E < 0.65
                             For JOO  <"s  <  BOO
                             0.30 < E < 0.45
                             For s">  BOO
                             E - 0. 30
                             Ul.ciu:
                             S « 10'  Ib bluam/lu
                             E = allowable  emission
                                 (Ib/lb exhauut  gas
                                  corrected lo  50Z
                                  eitcosd  air)

                   123-125   Source must  apply  to
                             stale for specific
                             emission limit lor
                             oilier titan coal burn-
                             ing sources
                                  Same as Existing
                                  Saiuu ati Existing
For I' <  30
E - 4.10(e)°'"
For P >  10
E - |55.0(l')'' "|-40
Uliere:
f =• process uulgltt
    (ton/hr)
E w allowable emission
      lO*1
       E - O.IU
       Where:
       () - bti.ii lj.|n.l  (I
           Illu/hr)
       t = allnuablu  uwl
                0fc Uln)
                                                             Know
                                                                                  t * allowable euilaaIon
                                                                                      (ll>/l>r)
                                                                                  I* = proeeaa weight
                                                                                      (tun/lir)
                                                                                                             None Knoun

-------
TAI1I.1-:  A-l   (Conlimied)
Stale A()CII i Combustion
EXISTING
M 1 s*ii»m" i "/O Kor 0^10 •
E = 0.60
For 10 < g < 10*
E » 0. B94 (O) ' '
For l| > lO*
E " 0.1B
Where:

Utn/br)
E " allowable emission
 10*
E - 0.19
Where:
f> g - heat Input (10'
1 Utu/lu)
' E a allowable emission
° (lb/106 Utu)
Nebraska 146 For g < 10
E - 0.60
For 10 < g < 3 BOO
E = 1.02u(<)) "*3)
For g > 3. BOO
E = 0.15
Uhe re :
g - beut Input (10°
lltn/hr)
E = allowable euiluslons
(lb/106 Ulu)
Units
NEW
For 0 < 10
E - 0.60
For 10 < g < 10*
E - 1.30J(IJ)"' ""2
For > 10*
E - 0. 10





For g < 10
E - 0.60
For 10 < Q < 10*
E - 1.026(Q)~'21J
For g > 10*
E - 0.12





For g > 2SO
E = O.lo









Process Units Catalytic Clunking Units
EXISTING NEW EXISTING NEW

E - ^.I0(l>)fl't/ UnlUi
For V > JO
(£ tt 155. 0(F)***' l-'iO
Uliuic;
P B( pructtiU weight
(l oiio/lu)
, . . . .
L ™ uliiiWitulu uiuluulun
(Ib/hr)


For 1* < 30 See Existing See Process Units See Process
E • 4.10 30
E =• 155.0(1')"' "1-40
Uhere:
P a process weight
(ton/hr)
E B allowable emission
(Ib/l.r)


For P < 30 See Process Units < 1.0 Ib/
E • 4.10(P)"'" 10' Ib of
For P > 30 coke buin-
E - |55. 0(1')"' "|-40 oil
Where:
P - process weight
(ton/hi)
E * allowable emission
(Ib/lir)



-------
TABLE A-l   (Continued)
Slate ACJCK t

Nevada









New llaiiitttjh 1 re 121











Combustion Units
EXISTING NEW
For Q < 2.5 See Existing
E = l.OU
For 2.5 < Q < 10'
E - l.M(Q) l>'2"
For Q > 101
E - U?9(Q) "'""
Uliere:
4 = beat Input
 10* For Q > 500
E •= 0.19 E - 0.10
Wbe re :
(| < beat lll|>ut (lO1 Ulo/br)
E - allowable euil:it 200
li ^ (4/10)
Ubere:
Q - beat Input (lltu/br)


For
E -
For
E -
Ube
1' '

E u


For
E -
For
E -
Process Unltu Catalytic Cracking Unllu
EXISTING NI'W EXIST1NC NEU
P < JO. 000 See Exltit Ing See Procebu Unltti See Process
O.T'JJd')0'" Hi. Ha
P > 30.000
111. 7«(lV " I-IU.K
re :
process uelgbt
(kllograus/lir)
allowable emission
(kllogra.us/br)


I1 > 30 For P > 30 -
1 66 .0(1') ** " * ' l-4b E = 155.0(1*)° *** I
Wbere: -40
p -

li =

-
For
t **
For
E -
For
E -
prutLJtia uuight
(iaim/hr>
ullawablij eml ^aloati
(Ib/hr)

0.5 Unlls
50 < K < '1000
K/IOO
H > 3000
3o7o
                        £ - allowable emluiiioii
                            (tb/lu
Uhutu:
H - uitcuitt rotluJ euilysiuna
    Ob/hr)
t •- atluwable cuifdalonu

-------
TAIil.K  A-1  (Continued)
State A1|CH 1 Coiuliubtlou Units
EXISTING NEW
New Mexico Coal Coal
For~0. < JO For l( < 250
E - 0.70 See Table In
For Q > JO Hegulallons
E " 0.50 For Q > 250
Where: E - 0.05
() - heal input (I0' lllu/hr) Oil

 1O1
E - 0.005
New Vurk 1 SB. 161. For Q < 10
162 E * 0.6
For 10 < (| < 10s
E * I.02(Q)"°' 2 "
For I) > 101"
E = 0.116
Uhere:
1) ' heat Input (H)b Utu/hr)
E = allowable emissions
(lb/106 lltu)
Nmih 0, < 10 Suiue as ExlBtliij
Carolina E = 0.60
1O < () < 100
E = 0.11
100 < Q < 1000
E " 5. IB
I) < 1000
E • 0. 10
Where:
t) - beat Input (10" lllu/hr)
db/br/lO1' Ulu)
Proeetjs Onllu Calalyllc Cracking Onllu
£5i5.'JliBfi HEU KX£S'rjNG NEW
402 opacity or < 0.02 grants/
< 100 Ib/hr dry SCF pluu
0.10 lb/101-
Ulu heal In-
pul I'roiu
uuxl 1 1 ary
fuel burilej





For 1' < 100.000 See ExItHlng See I'roueBS See Process
E = 0.024(1')°""* Uiiltu Uu 1 is
For 1' > 100.000
E - |J2(P)°''"'2|-50
Ul.uru;
P " proceus weight
Ub/hr)
E - allowable eiuis~
lilon (Ib/hr)

g For P < JO Saute ati Existing See Process See Process
E •= 4.10(1*)*'" Units Units
For P > JO
E - 155.0(1')"' ' ' |-40
Uhere:
P ** process welglil
(ion/In)
E - allowable ewlsslun
(Ib/l.r)



-------
TAUI.K  A-l   (Continued)
Slate Aljt:U I

North Dakota For
E =*
For
E "
For
E =
Whe
4 "
E >

Coiuboutlon Uiilttt
MiSi'LHt; NEU
1) < 10 See ExUllng
0.60
10 < O. < 101
o. an (ii) ••"'
<| > 10s
0.1B
re:
heat Input (10' Ulu/hr)
allowable emltiulon
(lb/hr/10* Ulii


For
E =
For
E =
Uhel
e =
•
E .-



^liM'n 1*1; h^y li* t5.'i'.iHi!
P < JO t>uuu> an ICxI ul iim Sue I*I"OI:CBU Uitl C a
4 .10(1') u " ** '
1* > it)
lS5.0(l*)fl* * ' |-AO
I't: «
JIIUL-Cba UiilgltL
(tun/lii )
ul luwub lu cmidii iua
(Ib/hr)

                                                                                                                                                               Ih.Uu
                          priority I
           lOi.li'i.lV'.    Kor  Q < 10                    Same an  EnUclng          Fur I1 < M                 Sutuc  ua  Enlacing    See 1'ruceus Unllb   See I'rucuuu
                          E =•  0.4                                                  E - 4.10(1') "•''''                                                      Unlm
                          for  10 < ()_< 10*                                         For V > JO
                          E =  O.B(IJ) <"1"                                         E " |S5.0(H)"-"|-40
                          For  I) > II)'                                              Where:
                          E -  0.1                                                  V - process weight
                                                                                        (iml/lrl)
                          i'rltif I iy II                                              E =• allowable  eutlutiloit
                          For  (j < 10
                          E '  0.6
                          For  10 < Q_< 1O1
                          E -  I.2«J) "' "'
                          For  1) £ 10'
                          E -  0.15
                          Where:
                          <1 -  heat Input  (lO*  Ulu/lu)
                          E =•  allowable euiluulon


                 U.lUtl   F lO1*
                          E =  0.1(1
                          Uliere:
                          I) "  heat Input  (IO0  Ulu/hr)
                          E ^  allowable eml uuloitH
                               (Ib/hr)

-------
TABI.Ii A-l   (Continued)
State Al)CU 1 Coubus 1 1 uu Uultu
EXISTING NKU
Oregon ly] 0.10 gralns/SCF 0.10 lb/10* IHu
I'eminy Is/an la 45 0.2 lb/101 Ib of mack 0.1 lb/101 Ib of
gad btack gad
Si ate St ate
•f E - 0.4
jjj For 50 <  600
E - 0.1
() - beat input <10L Utii/br)
(Ib/hr)
E - 0.20
Fur 0. > 250
E » 0.10
0 - lieat Input (!()' btu/hr)
E u allowable eiuiualons
(Ib/IO6 It in)
froce^u Unlta Catalytic Cracking Unllu
EXISTING NEW EX 1ST INC NEU
Fur 1' < 'JO See Exlutliig See rruceuu Unlls 1.0 lli/IO*
See table ill Kugula- Ib of coke
t luim burtiol 1 in
Fur P > JO regenerator
E = |55.0(P)"' "|-40
Where:
1' -= procesti weight
(tun/hr)
E " alluwable euilutilona
Ub/lir)
Fur V < 150.000 See Exlatliig < O.O2 grains/dry See Existing
E - 0.04 " or
For 150.000 < V < < 1.5d(l')°-l1'
300.000 Where:
Fur V > 300,000 (tuns of lli|iild
li - 0.02 feed/hr)
V ° Kltlii.Mit gau voluuui
(dry SCF)
E - allowable eiuluulontf
(grains/dry SCF)
E » 4.To(l')"'k7 Units
For P > 'JO
E - |i5.0(P)*'"|-40
Where:
P u pruceau weight
(tun/hr)
E c allowable euiisslon
(Ib/hr)

-------
TAUI.E A-l   (Continued)
Stale A<)CK »


Soul li Cu ro 1 1 nil tor
E -
Fur
E Je
aee
(( -
E "

Suutb llukula < 0.
In




E "
Fur
E *
For
E =
Wher
4 -
E "

< 0.
Fur"
E -
Fur
< o.
Coiubustlun llnltu
EXISTING NEW
Q< Ll\t\ "il'll fullil IlkW
•- *1UU Dull &Klbl lllg
0.60
Q > 400
peiulu UH utack liulght;
Flguiu 1 lu Uugulatlunti
llcul Input (III' bin/In)
allowable eiuiuuiuiiu
(lb/10C Blu)
JO lb/1011 Illu of heat Sue Existing
iput



Q < J (j yu r () < 10
0.6 E - 0.6
10 < l( < 10s Fur 10 < Q < 250
1.09(0.) °'2i"' E - 2.162(4)"°-6:"'
Q > I01" Fur <) > 250
0.1 E - 0.1
e:
heat iii|int (Hi* Utu/hi )
allowable euiitiulun^
(Ib/br)
J Ib/IO' Illu
1J ur Catf
Q < 2500
o.04a(i|)0' *2
I) > 2500
1 lh/10' Ulu
I'rucubu Unltb Catalytic Cracking llntlti
EXISiINC NKW EXISTINC NEM

li - 4.To(e)"'" Uilltu
Fur F > JO
E » (55. 0(e)"' ' ' |-40
Where:
E B allowable euilutilun
(Ib/hr)

fur V < JO See Exlutlng See Process Uilltu See I'rucess
E = 4.10(P)°'" Unllb
For P > JO
P - procebu weight (tun/hr)
E = allowable emluulun
(Ib/hr)
For 1' > JO For r > JO
E- |55.0(P)°'"|-40 E= 17. Jl(P)11' "
Where:
P = (iruceus weight
(tun/hr)
E & alluwahle ewltidl.uik
(Ib/br)

E =• 2574(1')''''°' Hulls
For P > 20
E = 1.12(1')"'""
Where:
P - proceuu weight
(lon/hr)
K = u) low able euiluu 1 uii
                         I) •-  heat  Input  (ID1  Ulu/br)
                         4 -  effluent  fluw  rate  (acfu)
                         E -  alluwable eiul^tilun  (Ib/hr)

-------
TABLE A-l   (Continued)
   Slulc
                AljCH t
                                          Couihusl Ion  Unllu
                                  EXISTlm:
                                                                MM
                                                                                             1'iocusii Hulls
                                                                                         EXISTING
                                                                                                                 NEW
                                                                                                                                        talulylli; Cracking Uulc;,
                                                                                                                                    EXISTINi:
               21'J,220     Coal
                           For Q > 10' Ul u/l.i
                           8SZ collection ef-
                           ficiency lu required
Veriitunl
                           For I) < 10
                           E = 0.5
                           For 10 < i) <  100
                                        See Enisling
                           For Q > MO-
                           E = 0.1

                           Q - heal Input  (IO'  IHu/lir)
                           E = allowable emission
                                       Bio)
                                                                 See 'fable  1  In
                                                                 Regulations
                                                                                         See Enlacing
                     See I'rocetiu Unllu  See  I'rocet;^
                                        tli.llb
Virginia
22J    Stale
       For Q <  25
       E - 0.4
       For 25 < <(  <  10s

       For Q >  10*
       E - O.I
       Ul.ere:
       1) * lieal liunil  (I0k  Ulo/hr)
       E - allowable euilbulony
           (lb/10' Ulo)

       AljCK 221
       For 1) <  B/
       E = 0. J
       For 87 < Q  <  10s
       E = 0.8425(l))""';"1''
       For I) >  I01*
       E - 0.1
                                                            Scu Kalutlng
                                                                                     Stale
                                                                                     For P < '10
                                                                                     E = 4.10(P;
                                                                                     For p > 10
                                                                                     E = |5
                                                                                     Where:
                                                                                     1' = )>roceiiS welghl
                                                                                         (ton/hr)
                                                                                     E = allowable eiulutilon
                                                                                         (Ib/hr)

                                                                                     AIH-H 22'1
                                                                                     See Table 4.408  In
                                                                                       Uegtilal loikti
See Enltillng         < O.OSZ of ihe      See  Enisling
                     caialyui reclrco-
                     lallon rale wlihln
                     the onlt
Virgin Island*      247

-------
TAUI.K  A-l   (Continued)
   Scale        AljCK »
Washington    193.22U.
                  229
                                          Couibotil lull UnlCti
< 60 t1 Braius/H   as  an
annual geometric uieaii
                                                                NKU
                                                                                             Procu^u  Uulra
                                                                                        liXISTINC
                                                                                                                NtW
                                                                                                                                      Calalyllc  ^r
                                                                                                                                                          Uulta
                                                                                                                                   KXISTINi;
Went          179.234
  Virginia
Kor Steaui Ceneral Ion
E = 0.05 ()
  not to exceed  1200

Other Heat Inn
E " 6.09 ()
not to exceed 600
Where:
g = total design lieut  Input
    do' Utu/hr)
E = allowable emissions
    Ub/hr)
See Existing
Kor 10 < f.<  100
E - 0.22 P-0.4
Kor P > 100
E = 21.5
Where:

    (101 Ib/hr)
£ = allowable emission
    (Ib/hr)
                                               See Existing
See Pmcesu Units     See Process
                        Units
Wisconsin
                            Kor g < 25O
                            £ - 0.15
                            Kor  250
                            E = 0.10

                            I) •- heut Input (II)' Uto/hr)
                            E a allowable eiuluulons
                                (I0' lltu/hr)
                                                     for  I'  <  30
                                                     E  -  3.59(1'
                                                     Kor  V  '  30
                                                     E  =  1
                                                         (toil/hi )
                                                    E =  allowable eml salonti
                                                         (Ib/hr)
                                                                                                               liiUcluts
                                                                   1.0  Ib/IO* ol coke   See
                                                                   burn-off In catalyst
Wyouil ng
Kor I) < 10
E = 0.10
Kor 10 < Q <  iO11
£ - .8963(1))"°' ' Mi
Kor g > 10*
£ - 0.18
Uhere:
g -= heut Input  do'  Utu/hr)
E = allowable emission
         Ub Utu)
                                                                                Kor Y < 30
                                                                                E • 4.10(tV"
                                                                                Kor V > 30
                                                                                E. - 155.0(f)'""|-<,0
                                                                                Where:
                                                                                E - allowable uiultis Ion
                                               Kor I' < 30
                                               E - 3.590')0"2
                                               Kor F ' 30
                                               E * IV.riKl')''"
                                              See frocesu Units     See 1'focess
                                                                    Units

-------
TABLE A-2.	APPLICABLE SULFUR COMPOUND REGULATIONS
Combustion Units
Stnte AQCR0 Existing New
Alabama 2,4 4.0 lbs/106 Btu heat Input 1.8 lbs/106 Btu heat
input
5 4.8 lbs/106 Btu heat Input
2.4 lb/106 Btu heat input Same as Existing
for modified sources
Alaska 8,9 500 ppm as S02 See Existing
Arizona 14,15 <1.0 lbs/106 Btu heat input <0.80 Ibs/ 106 Btu
for low sulfur oil input for low sulfur
oil
<2.2 lbs/106 Btu heat input
for high sulfur oil
Arkansas . 18,19 <0.20 ppm S02 (30 rain. avg. See Existing
outside premises)
California 24 Gaseous fuel must be <300 ppm See Existing
HjS at stand, cond . Solid and
> liquid fuels must be <0.5% S
' by weight
GO
29 All Sources: <0.05% by volume See Existing
as SO?
Caseous fuel must be <10 grains
S/100 ft3 (calculated as II2S)
Solid fuel must be <0.5Z S by
weight
30 <300 ppm at all times See Existing
31,32 £200 Ib/lir See Existing
Colorado 35,36 Solid Fuel See Existing
1.2 Ib S02/106 Btu
Liquid Fuel See Existing
0.8 Ib S02/106Btu
Connecticut 41 <0.5% S In any fuel by See Existing
weight, dry
Process Units Sulfur Recovery Units
Existing New F.xistlng New
None None 0.08 Ibs S()2/lb of
sulfur processed
None
2,000 ppm 112S 500 ppm 112S 0.12 Ibs S02/lb of
sulfur produced
500 ppm as S02 See Existing See Process Units See Process Units
<10% of sulfur See Existing See Process Units See Process Units
entering ae feed
See Combustion See Existing See Combustion Units See Combustion Units
Units
<500 ppm S02 See Existing See Process Units See Process Units
£10 ppm 1I2S
<500 ppm <500 ppra See Process Units See Process Units
See Combustion See Combustion .04 ppm ground level See Existing
Units Units concentration (24 hr
avg.)
<2000 ppm <2000 ppm <2()00 ppm £2000 ppm
<500 ppm S02 <500 ppm S02 See Process Units See Process Units
<500 ppm S02 <500 ppm S02 See Process Units See Process Units
<5()0 ppm See Existing <0.0i Ib S/lb S See Existing
processed

-------
                                                TABLE A-2 (Continued)

State
Delaware
Florida
Georgia














Hawaii





Idaho




Illinois





AQCK0 Existing
45 See Pennsylvania
5 See Mississippi
2,49,56 <100 x 106 Btu/hr
58 Units — maximum
2.5% S by weight
in fuel allowed



>100 x 106 Btu/hr
Units — maximum 3%
by weight in fuel
allowed




60 <2% S in any fuel
by weight, dry
>250 x 106 Btu/hr
Heat Input must burn
fuel <0.5% S by
weight





67,70,74 1.0 Ibs S02/106 Btu
of actual heat input
for residual fuel
0.3 Ibs SO 2/10 6 Btu
of actual heat input
fnr ili a t- i 1 1 nl-o funl
„ . . ... T'rnrpsq iinlrs Sulfur Recovery Units
Combustion Unlf*i rot-ess unii-b . 	 j 	 . 	
New Existing New ExlstliiR New


Coal Oil

E = 1.2 E = 0.8 See Combustion
Where: Units
E = Allowable
emissions
(lb/J06 Btu)
Also
For Q <100
5 2.5% S Fuel
For Q > 100
£3.0% S Fuel
Where:
Q = heat input
(106 Btu/hr)
See Existing





Solid Fuel <0.1 grain !I2S/ See Process Units
dry SCF in any
<_ 1.2 lb/106 Btu fuel gas
Liquid Fuel
£0.8 ih/10c Btu
>250 x 106 Btu/hr 2000 ppm S02 2000 ppra S02 2000 ppm S02 2000 ppm S02
Units

0.8 Ibs of S02/
1 C\ U 1- 1 1 rtf -10 t- i i n 1
Units burning
gaseous fuels only
are exempt from
regulations
heat input for
residual oil

0.3 Ibs of S02/
JO6 Btu of actual
heat input for
distillate oil

-------
                                                                                 __IMLj Ar2_(CqjVj:lpijied)
ro

State
Illinois
(cont 'd. )






Indiana






Iowa



Kansas


Kentucky















Combustion
AQCK// Existing








77,80,
81 Em - 17.0 Qm
Em = Ibs S02/106 Btu
Heat input

Qm ™ Heat Input in
106 Btu/br
6.0 >_ Era >1.2
65 Solid Fuel
£3 Ib S02/106 Btu
Liquid Fuel
<2.5 Ib SO2/10C Btu
94,96, For heat Input >
97,98, 250 x 106 Btu/hr,
99,100 £1.5 Ib S/106 Btu
78,103, Solid Fuel
105 Class 1 „ ,,,,
E = 13, 878 (Q)~ '
Class I.I n -.-.,
E = 14.1967 (Q)"
Class III 3
E - 12.254 (Q) u'^'Ji
Class IV , ....,„
E - 10.8873 (Q)-°-1338
Class V _ ,,
E = 12.0284 (Q) '
Liquid Fuel
Class 1 „ , .„,
E - 7.7223 (Q)-°-A106
Class 11 « ....
—0 3/4
E = 9.4644 (Q) J *
Class [II _0.2A36
E = 8.06 (Q)
Unlts Process Units Sulfur Recovery Units
New Existing New Existing New
<2.50 x 106 Btu/hr
Units
1.0 His S02/106 Btu
of actual beat input
for residual oil
0.3 Ibs SOz/lO6 Btu
of actual heat input
for distillate oil
0.67
See Existing Ep = 19. 5P See Existing See Process Units See Process Units
lip = Ibs S02/hr

P " Total process
capacity tons/
br

Solid Fuel 500 ppm S02 500 ppm S02 See Process Units See Process Units
£1.2 Ib S02/106 Btu <0.1 grain II2S/
Liquid Fuel dry SCF gaseous
£0.8 Ib S02/106 Btu fuel
See Existing


Solid Fuel <2000 ppm See Existing See Process Units See Process Units
For Q <10 and
E - 5.0 <0.1 grain H2S/
For 10 <() <250 dry SCF
E = 9.4644 (Q)
For (} >250
E = 1/2
Liquid Fuel
For Q <10
E = 3.0
For 10 250
E = 0.8






-------
                                                              TABLE A-2 (Continued)
   State	AQCR
Kentucky
(cont'd.)
LouLsian.i      106
Mill lie
109,

110
Maryland       115, 116
Massachusetts   42
               119
Michigan       122
               123-125
Minnesota      129, 111,
               132
Mississippi      5
                                      Combustion Units
                                                                                         Process  Units
                            Existing
                                                                                  Ex lating
                          .-O.I 3/i 7

                          ,-0.126
Class IV
 E - 7.364 (l))"
Clans V
 E = B.019 (Q)~
Where:
Q = heat input (106 Btu/hr)
E = allowable emission
    (lb/10c Btu)

<2000 pptu by volume
at standard conditions
<2.5% S In fuel

<1.5Z S In fuel
            <0.5Z S  in  residual
            <0.3Z S  In  distillate
                                                          See Existing
Solid Fuel
£1.2 lb/10' Btu
Liquid Fuel
<0.8 lb/10r Btu

See Existing
            <0.55  Ib  S/IO'  Btu  of
            heat  Input—coal  and
            residual  oil

            <0. 17  Ib  S/106  Blu  of
            heat  input—No.  2 fuel
            oil                               See Existing

            <0.28  Ib  S/106  Htu  of
            heat  input—coal  and
            residual  oil

           ' For U S  fuels
            Liquid—420 ppm or  1.1  Ib  SO2/106  Btu
            Solid—590 (ipm  or 1.6  Ib SO2/10fi  Btu
            For 1.5%  S fuels
            Liquid—630 ppm or  1.7  Ib  SO2/106  Btu
            Solid—890 ppn  or 2.4  Ib SO2/lo'  Btu
            For 2Z S  fuels
            Liquid—840 ppm or  2.2  Ih  SO2/10*  Btu
            Solid— 1180 pom  or 3.2 Ib SOj/lO6  Htu
             See Table  I  In
             regnlat ions

             4.8 lbs/106  Btu
             2.4 lbs/10b  Btu  for
             modified sources
                                 See Table 2  In
                                 regulations
                                                                  <2000 ppm by  volume   See Existing
                                                                  at  standard con-
                                                                   ditions
                                                                                 None
                                                                                 2000  ppm  S02
t£0.1 grain
dry SCF
                                                                                                      500  ppm SO2
                                                                                    <25  ib/hr
                                                                                    <500 ppm
                                                         30U  ppoi  for  any
                                                         source
                                                         100  grains II?S/
                                                         100  ft1  for  pro-
                                                         cess gas streams
                                                                            <25  Ib/hr
                                                                            <500 ppm
                                                         r2l)00  ppm
                                                         <1  grain  II2S/
                                                         100 SCF
                                                                                                       500
                                                                                                       	Sulfur Recovery  Units	
                                                                                                        Existing	      New
                                                            <0.01 Ib/lb  S
                                                             Processed or <1300
                                                             ppm SO2

                                                             None
                                                                                                                                              See  Existing
                                                                                                                                              See  Process
                                                                                                                                              Units
                                                                                            95Z Reduction of      See Existing
                                                                                            SOa emissions from
                                                                                            the plant
                                                                                                                        See Process Units
                                                             0.02  Ib SU2/lbs
                                                             produced
                                                                                                                                               See Process Units
                                         0.01 Ib SO2/lbS
                                         produced
                                                            10.12  Iba S02/lh  S
                                                             produced
                                                                                                                                               Sec Existing
                IH
            ('nnnot exceed  1970
            em Issions

-------
                                                                              TABLE A-2  (Continued)

State
Missouri
Montana

Nebraska

AQCR 9
70
140, 141
143
146
Combustion
Existing
See Illinois
, Liquid or Solid Fuel
£1.0 Ib S/106 Btu
Caseous Fuel
<0.5 grains S/SCF
2.5 Ib S02/106 Btu
Units
New
Solid Fuel
<1.2 Ib S02/10l'Btu
Liquid Fuel
£0.8 Ib S02/106 Btu
See Existing
Process
Existing


Cannot exceed
1972 emissions
Units
New

<0.1 grain I12S/
d7y SCF
See Existing
Sulfur Recovery Units
Existing New

<0.1 grain 1I2S/
dry SCF
Sec Process Units See Process Units
      Nevada
                                 For  Q  <250                     See  Existing
                                 E  =  0.7Q
                                 For  250 £Q  <5,000
                                 E  =  0.4Q
                                 For  Q  >5,000
                                 E  =  0.105Q
                                 Where
                                 Q  =  heat  input  (106  Btu/hr)
                                 E  =  allowable emissions  (Ib/hr)
                                                     E = 0.292(P)~°'904 See Existing
                                                     Where:
                                                     P = total feed
                                                         sulfur (Ib/hr)
                                                     E = allowable emis-
                                                         sion (Ib/hr)
                                                                                                                             See Process  Units   See Process Units
       New Hampshire   121
 I
NO
       New  Jersey

       New  Mexico
<0.4% S by weight-
No. 2 fuel oil

<1.0% S by weight-
No. 4 fuel oil

<2.0Z S by weight—
No. 5 and No. 6 fuel oil

<5 grains HjS/lOO SCF gas

<310 ppm S02

Coal
For Q >250
E = 0.34
Oil
For Q >106
E = 0.34
Where:
Q = heat input (106 lltu/hr)
E = allowable emission
    (lb/10G Btu)
See Existing
Maintain ambient
standards
See Existing
                                                                                                                             See Process Units   See Process Units
See Existing

Coal
For Q >3,000
E £102, hy weight
 S02 produced by
 combustion
<2000 ppm SO2

For A >5
10 Ib S/100 Ib S
released In plant
processes
Where:
A = average
    release of
    sulfur in
    plant pro-
    cesses (ton/
    day)
See F.xisting

For 5 £A <30
10 Ib S/100 IbH
For A >30
2 Ib S/100 Ib S
and
£0.1 grain I12S/
SCF fuel gas
                                       15,000 ppm SO2

                                       £12 Ib S/100 IbS
                                       Introduced into
                                       the plant
                                        See Existing

                                        £10 ppra II2S or
                                        TT2S of effluent
                                        gas stream is
                                        oxidized to S02
                                        and
                                        for A <20
                                        E = 10 Ib
                                            S/100 Ib S
                                        for A >20
                                        E = 2 Ib S/100 IbS
                                        Where:
                                        A = sulfur intro-
                                            duced into
                                            the plant
                                            (ton/day)
                                        E = allowable emis-
                                            sion (Ib S/lb S
                                            introduced)

-------
                                               TABLE A-2  (Continued)
Combustion
State AQCR Existing
New York 158, 161, 0.75 wt % S in oil
162 50 grama I12S/100 SCF gas
North Carolina 2.3 Ib -SOa/lO6 Btu
North Dakota 3.0 Ib S02/106 Btu
Ohio 103 See Kentucky
12/i See Michigan
174, 177, Priority I
181 E » 1.0
Priority II
E = 1.6
Priority III
E = 3.2
Where:
E = Ib S02/106 Btu
Oklahoma 17, 188 <1350 (Jg/ra3
J> (0.52 ppm) at
1 any point in
f^ 5 mln. ;
LO
<1200 |ig/m3
(0.46 ppm)
1 hr. avg. ;
<650 |ig/m3
(0.25 ppm)
3 hr. avg. ;
<130 |ig/m3
(0.05 ppm)
24 hr. avg.
Oregon 193 Solid Fuel
For 150 250
Units
New
See Existing
1.6 Ib S02/106 Btu
See Existing
See Existing


Gas Fuel
<0.2 lb/10" Btu
heat input
Liquid Fuel
<0.8 Ib/.l.O8' Btu
heat input
Solid Fuel
<1.2 ib/106 Btu
heat input
Solid Fuel
E = 1.2
Liquid Fuel
E = 0.8
Process Units Sulfur Recovery Units
Existing New Existing New
*
<50 grams IIjS/100 See Existing See Process Units See Process Units
SCF
Maintain Ambient Air Quality See Process Units See Process Units
Standards
2000 ppm S02 500 ppm S02 <0.01 Ib S02/lb S See Existing
processed

See Combustion See Combustion <20 Ibs S/ton
<0.1 ppm I12S, <0.3 Ib U2S/hr, Processed, max.
30 mln. period 2 hr. max., 95Z 2 hr. avg.
max. efficiency
of I12S in exhaust
gas unless >100 Ibs
S02 would be dis-
charged, max. 2
hr. avg.
<0.10 grain M2S/dry See Process Units
SCF
E = 1.2
Liquid Fuel
For 150 «) <750
E = l.t,
For Q >250
E = 0.8
Where:
Q = heat Input (106 Btu/lir)
K = allowable emission  (lb/106  Btu)

-------
                                                                      TABLE, A-2  (gonginued_)_
Combustion Units Process Units Sulfur Recovery Units
State AQCR0 Existing
Pennsylvania 45 <0.2% S for No. 2 fuel oil
<0.3% S for other fuel oil
or 0.3 Ibs S02/106 Btu
or <310 ppm SOz
Rhode Island <1.1 Ib SOa/106 Btu
South Carolina Class 1 County
Q <10
E = 3.5
Q >10
E = 2.3
Class II. County
E - 3.5
Q HO3
E = 2.3
Class III County
E = 3.5
Where:
Q = heat input (106 Utu/hr)
^* E = allowable emission
fV, (lb/106 Btu)
South Dakota £3.0 Ib S02/106 Btu
Tennessee 7 4.0 lbs/106 Btu of
heat Input
Texas 22, Fossil Fuels, Solid:
210-1218 <3.0 Ib S02/10" Btu
heat input
Steam, Liquid Fuel
<440 ppm SO 2
by volume
Utah 219, 220 Coal
<1.0 weight 1 S
Oil
<1.5 weight Z S
New Existing New Existing New
See Existing 500 ppm S02 See Existing Some as Process See Existing
See Existing
See Existing
See Existing Maintain Ambient Air Quality See Process Units See Process Units
Standards
<250 x 10G Btu/hr 2000 ppm 2000 ppm See Process Units See Process Units
4.0 lbs/106 Btu
of heat input
>250 x 106 Btu/hr
Federal Standards
New sources must See Combustion See Existing For Q <4000 See Existing
meet any appll- Units E = 123.4 + 0.091 Q
cable new source For Q >4000 Q 8042
performance stand- '*l
ard and utilize E = O.fil4
beat available E = Ib S02/hr
control technology (} = effluent flow
rate (scfm)
Coal Maintain Ambient Maintain Primary See Process Units See Process Units
<1.2 Ib S02/106 Air Quality and Secondary
Btu Standards Ambient Air
Oil Quality Standards
<0.8 ll> S02/106 and
Btu <0.l grain HaS/dry
SCF
Vermont
                           <2.0 weight 7. S
Sec Existing

-------
                                                                            TABI.E A-2
        State
              AQCR0
                                              Combustion Units
                                                                                         Process Units
                                                                                                                                   Sulfur Recovery Units
                                    Existing
                                                                 New
                                                       Existing
                                                                                                            New
                                                                  Existing
                                                                                                                                                        New
    Virginia
              223
               47
E = 2.64 Q
E = 1.06 Q
Where:
Q = lieat input (106 Btu/lir)
E = allowable emission
    Ub/hr)
Coal
£1.2 Ib S02/106 Btu

OU
<0.8 Ib S02/106 Btu
                                                                 <2000 ppm
£2000 ppiu
and
£0.1 grain II2S/
dry SCF
£8000 ppm and
K = 8.3 1'
Where:
P - sulfur production
    (ton/day)
E = allowable emis-
    sion (Ib/hr)
                                                                                                                                                  See Existing
    Virgin
     Islands

    Washington
                  247
193, 228
229
                          2000 ppm SO2
                          1000 ppm SO 2
 I
K3
Ln
West Virginia 179, 234    Priority I & II Counties
                          E = 3.1 Q
                          Priority III County
                          E = 3.2 Q
                          Where:
                          Q = total unit heat
                              inputs (10  Btu/hr)
                          E = allowable emissions
                              (Ib/hr)

Wisconsin                 Maintain Ambient Air
                          Quality Standards
    Wyoming       241-243     For 250 £ Q <2500
                              E = 1.2
                              For 2500 £ Q <5000
                              E = 0.5
                              For Q >5000
                              K = 0.3
                              Where:
                              () = heat input (106 Btu/hr)
                              E = allowable emission
                                  Oh/106 Btu)
                              1000 ppm S02
                                                            All Counties
                                                            E = 2.3 Q
                                                            and
                                                            E = <8,000 Ib/hr
                       2000 ppm or >40
                       lbs/hr sources
                       can only emit 10% <
                      | of S contained in
                      I process wt/hr

                       <2000 ppm
                                                                                                      1000 ppm SO?
                                                                        <2000 ppin
                                                                                                                          Same as Combustion Units
                                                                                                        £0.06 Ib S02/lb S
                                                                                                        processed
                                            See Existing
Solid Fuel <0..1 grain II2S/
<1.2 Ib S02/106 Btu dry SCF
Liquid Fuel
<0.8 Ib S02/10C Btu
For q >250
Coal
I -"l.2
Oil
E - 0.8
See Process
Units

-------
                            TABLE A-3.   APPLICABLE NITROGEN  OXIDES REGULATIONS
  State
                  AQCR
             Combustion  Units
                                               EXISTING
                                                                                                 NEW
Alabama
                     2
                     4
                     5
                     7
None
> 250 x 106  Btu/hr
0.2 lbs/106  Btu of heat  input  for  gas-fired
units
0.3 lbs/106  Btu of beat  input  for  oil-fired
units
Alaska
                     8
                     9
None
None
>
ro
Arizona
                   15
                                                   None
                          0.2  lbs/106 Btu of heat input for gaseous-
                          fired units
                          0.3  lbs/106 Btu of heat input for oil-fired
                          units
Arkansas
                    17
                    18
                    22
                                                 None
                                                                          None
California
                   31
                   29
                   30
                                       125 ppm NO   in  flue gas for
                                       gas-fired units
                                       225 ppm N0x  in  flue gas for
                                       oil-fired units

                                       125 ppm gas-fired  units
                                       225 ppm oil-fired  units
                          125  ppm HO  in flue gas for gas-fired units
                          225  ppm N0x in flue gas for oil-fired units
                          Maximum emission rate of NOz < 140 Ib/hr
                          Same  as  Existing

-------
TABLE A-3   (Continued)
  State
AQCR It
                   35
                   36
             Combustion Units
Colorado 14
EXISTING
None
NEW
None
 Connecticut
                     0.2  lbs/106  Btu of heat input
                     for  gaseous-fired units
                     0.3  lbs/106  Btu of heat input
                     for  oil-fired  units
                          Same  as  Existing
 Delaware
  45
None
                    None
 Florida
   5
  49
  50
None
> 250 x 106 Btu/hr
0.2 lbs/106 Btu of heat  input  for  gas-fired
units
0.3 lbs/106 Btu of heat  input  for  oil-fired
units
 Georgia
   2
  56
  58
None
> 250 x 106 Btu/hr
0.2 lbs/106 Btu of heat  input  for  gas-fired
units
0.3 lbs/106 Btu of heat  input  for  oil-fired
units
 Hawaii
  60
None
                    None

-------
 TABLE  A-3   (Continued)
   State
AQCR //
                          Combustion Units
 Illinois
  67
  73
           EXISTING

> 250 x 106 lltu/hr heat input;
0.3 lba/106 litu of heat input
for liquid and gaseous fuel
                                                                                                  NEW
> 250 x 106 Btu/hr heat input units:
0.2 lbs/106 Btu of heat input for gaseous
fuels
0.3 lbs/106
fuels
                                                                                          Btu of  heat  input  for  liquid
                    70
                    73
                                 None
                                        Same  as  above
 Indiana
i
K>
OO
  67
  80
  81
> 250 x 106 Btu/hr heat input
units:
0.2 lbs/106 Btu of heat input
for gaseous fuels
0.3 lbs/106 Btu of heat input
for liquid fuels
Same as Existing
 Kansas
  96
  97
  98
  99
> 250 x 106 Btu/hr oil or gas
fired:
0.3 lb/106 Btu
Same as Existing
 Kentucky
 103
 105
             None
> 250 x 106 Btu/hr
0.2 lbs/106 Btu of heat input for gas
fired units
0.3 lbs/106 Btu of heat input for liquid
fired units

-------
TABLE A-3   (Continued)
  State
AQCR fl
                          Combustion Units
                                                EXISTING
                                                                               NEW
Louisiana
  22
 106
             None
                   None
Maine
 109
 110
             None
                   None
Maryland
 115
 116
             None
For units > 250 x 106 Btu/hr:
0.2 Ib N0x/106 Btu for gas-fired units
0.3 Ib N0x/106 Btu for oil-fired units
Massachusetts
                  119
                  121
Michigan
 122
 124
             None
                   None
Minnesota
 129
 131
 132
For gaseoua units with a capacity
of 250 x 106 Btu/hr or greater:
0.3 Ibs of N0x/106 Btu input/hr
For oil-fired units with a capacity
of 250 x 106 Btu/hr or greater:
                                     0.4  Ibs of N0x/10l
                                       Btu input/hr
For gaseous units with a capacity  of
250 x 106 Btu/hr or greater:
0.2 Ibs of N0x/106 Btu input/hr
For oil-fired units with a capacity of
250 x 106 Btu/hr or greater:
                                        0.3  Jba  of N0x/10*
                   Btu input/hr

-------
  TABLE A-3   (Continued)
    State
AQCR //
             Combustion  Units
                                                 EXISTING
                                                                              NEW
  Mississippi
   5
  18
None
None
  Missouri
  70
None
None
  Montana
 140
 141
None
None
i
Co
o
  Nebraska
 146
  New Hampshire      1.21
None
                                None
None
                                            None
  New Jersey
  43
  45
None
None
  New Mexico
  14
 153
None
None
  New York
  43
 158
 161
 362
None
None

-------
  TABLE A-3   (Continued)
   State
AQCk //
                           Combustion Units
  North  Dakota  •    172
                                                EXISTING
                                 None
                                                           .NEW

                                                           None
  Ohio
 103
 124
 124
i
LO
For gaseous-fired units with a
capacity of 250 x 106 Btu/hr or
greater:
0.20 Ibs of N0x/106 Btu input per
hour
For oil-fired units with a capacity
of 250 x 106 Btu/hr or greater:
0.30 Ibs of N0x/106 Btu input per
hour
Same as Existing Sources
 Oklahoma
  17
  22
 186
 188
              None
For gaseous-fired units with a capacity of
50 x 106 Btu/hr or greater:     r'
0.20 Ibs of N0x/106 Btu/hr
For oil-fired units with a capacity of
50 x 106 Btu/hr or greater:
0.30 Ibs of N0x/106 Utu/hr
 Oregon
 193
              None
                                                                              None
 Pennsylvania      45
                  178
                  197
                                None
                                        For  units  >  250 x  10b Btu/hr:
                                        0.2  Ib N0x/106 Btu  for gas-fired units
                                        0.3  Ib N0x/106 Btu  for oil or gas-fired
                                        units
 Tennessee
   7
  18
              None
Comply with Federal Standards

-------
  TABLE A-3   (Continued)
    Slate
AQCR II
                            Combustion Units
  Texas
u>
ho
 215
 216
  22
 106
 153
 210
 21.1
 212
 213
                   217
                   218
            EXISTING

For gas-fired units greater than
800 million Btu/hr input:
"opposed fired" - 0.70 Ibs N0x per
10* iltu/hr
"front fired" - 0.50 Ibs N0x per 106
Btu/hr
"tangential fired" - 0.25 Ibs N0x
per 10G Utu/hr

              None
                                                                                               NEW
Same as Existing
                                                                                              None
  Utah
 219
 220
              None
             None
  Virginia


  Washington
 223
 193
 228
 229
              None
              None
             None
             None

-------
   TABLE A-3   (Continued)
     State
AQCR It
                            Combustion Units
                                                EXISTING
                                                                             NEW
  West  Virginia
 193
 228
 229
              None
             None
  Wisconsin
 129
              None
> 250 x 10b Btu/hr units:
0.20 Ibs of N0x/106 Btu of heat  input
for gaseous fuels
0.30 Ibs of N0x/106 Btu of heat  input
for oil fuels
coUyoming
CO
 241
 242
Gas-fired: 0.23 lb/106  Btu
Oil-fired: If beat input  < 250 x 10e
Btu/hr
0.60 lb/106 Btu
If heat input > 250 x 106 Btu/hr
0.46 lb/106 Btu
Gas-fired: 0.20 lb/106  Btu
Oil-fired: 0.30 lb/106  Btu

-------
                                                              TABU; A-4.  APPLICABLE IIYUKO<:AKUON RKCULATIONS
 I
Co
State

Alabama
Alaska
Arizona
Ca liiornla

AQCKtf Loading Kacks
lixi sting
2 for racks handling
4 50.000 guls a day
5 or wore, a vapor
7 recovery system in
good working order
is required.
8 None
y
Existing
15 Submerged fill or
equivalent for 1.5
pala or greater
24 Los An^el us Co.
New
Oil-Water Catalytic Vapor
Separation Ke^enei atom Blowdown
Existing
if unit handles 1.000 None None
gals a day or uiore of
volatile organics.
unit must be equipped
with a solid or float-
ing cover , a vapor
equ Ivalent method .
None None None
None None None
Existing Existing
                                              >20,000 gal/day-
                                              uiimt have vapor col-
                                              1ect ion and disposai
                                              systeiu or equivalent
                                              u/902 by weight
                                              recovery or vapor
                                              handling system or
                                              other equipment of
                                              equal efficiency
                                              (v.p.> l.Spai)
>200 gal/day petroleum
products, v.p.  0.5 psl
or greater - vapor
lose control device
required.
Safety pressure relief
valves - v.p.>15.0 psl.
Must be vented to
vapor recovery or
disposal system pro-
tected by a ruptured
disc or maintained by
approved Inspect ion
plan.
                                                                                                                                                       Storage
                                                                                                                                                  Floating roof or
                                                                                                                                                  vapor recovery for
                                                                                                                                                  tanks of 60,000
                                                                                                                                                  gals or more
                                                                                                                                                  storing volatiies
                                                                                                                                                  (1.5 psla or greater)
                                                                                                                                                    Existing
                                                                                                                                                  >65,000 gal.-pressure
                                                                                                                                                  tank or vapor recovery
                                                                                                                                                  (2.0 paia or greater)
                                                                                                                                                  All new tanks submerged
                                                                                                                                                  fill or equivalent
Existing

>40.0QO gai-v.p.
>1.5 psl absolute-
pressure tank or vapor
loss control devIce.
vp 1i.0 pal, can't use
floating roof.

>40.000 gal-v.p.
15.0 psi - pressure
vacuum valve.
>250 gal exempt.

Crude Oi1 exempt
If <150 Ib/day non-
methane or nen-ethane
hydrocarbons.
Existing
<2000 gal exempt.

-------
                                                                         JVVB1.E A;_«.	 (Continued)
State
California


AQCRS Loading Racks
24 Southern California APCD
New
>20,000 R/d (>1.5
psla) - must have
Oil-Water
Separation

New
>201g petroleum pro-
ducts. >0. 5 psla -
Catalytic
Regenerators


None
Vapor
B lowdown

F.xlHtlng
>15 Ibs/psla-must be
Storage


>25I g: must h;we
•JOZ bv weight vanor
                                     29
 I
U>
Ul
vapor collection and
disposal system or
equivalent

<20,00() g/day but
>500,000 g/annnally
must return displaced
vapors to storage tanks
from delivery vessel.
Must have submerged
fill when liquid level
is 3.J5 Jn.  above
vessel bottom.
must have sol id cover
w/sealed openIngs,
floating roof, or
vapor loss control
device.  Vapor re-
covery system w/90%
by weight recovery.

Crude oil separators
exempt if water has
<5 ppm \\2%, organic
sulfides, or combi-
nation.

New

>200 b/day petroleum
products w/Keid v.p.
of >0.5 Ib - must have
vapor loss control
device.  Crude oil
facilities - exempt
If water has <5 |>pm H?S
organIc sulfides, or
comb inatlon.

Existing

Same as new after 1/1/74
                                                                                                                      covery or  disposal
                                                                                                                      system protected  by
                                                                                                                      a  ruptured disc or
                                                                                                                      maintained by
                                                                                                                      Inspection system
                                                                                                                      (2000g/month output-
vapor JOBS control device
or equi va lent for -"1 . r) ps I a
(unless exclusi vely used as
source of fuel for agr (cul-
tural wl nd mac 1 1 lues .

Exist ing

>550g size container or
>2000 g/immi:h output-same
as new after  12/1/74.
<2000g/mo nnd suhm<-rgi:d
fill-no other control n
-------
	State

California
AQCKtf

   30
                   35
                   36
>
U>
Connect lent
                 41
  l.oad I UK Hacks

EaistinK

500-25,000 gal/day
w/^4 Held v. p. and
heat apace reactivity
>5X Into containers
>100 g.-reduce by 90Z
                                                              Oil-Water
                                                              Separation
                                                                 Catalytic
                                                                         Vapor
                                                                         Ulowdown
                                                         Existing

                                                         >200 g/d, less than
                                                         40l°F teuip. at IUZ
                                                         point recovered, head
                                                         space reactivity  5X
                                                         •^0.21 vol. or organic
                                                         1Iquid recovered.
            Equipped wltli vapor
            collection and dis-
            posal system In good
            working order.  Prevent
            drainage from loading
            device when removed.
            System to remain vapor
            t Iglit at all times.
            Collection equipment
            not to exceed 1.24 lb.;i.
            vapor emission per .1000
            gulu j oaded.  If less than
            20,000 gal. per calendar
            day loading exempt from
            vapor recovery rei|ul reuient,
            but must have 97Z submerged
            fill.

            Existing

            > 10.01)0 g/day loading
            >200 g capacity contain-
            ers-vapor collection and
            disposal system, loading
            arm u/vapor-tight seal,
            no leakage; if means other
            than hatches used - vapor
            tighc lines requlred.
                                                         If unit handles 200 gals
                                                         or more per day of organic
                                                         materials with Held vapor
                                                         pressure >0.5 pound, must
                                                         have vapor tight solid
                                                         cover, floating roof, or
                                                         vapor recovery and d1s-
                                                         poaal system.
                                                                                                                                       Storage
                                                         >200 g/d - vapor recovery
                                                         required or equivalent
                                                                                      None
                                                                         Smokeless flares or
                                                                         equiva lent.
                                                                                                                Existing

                                                                                                                <1000 barrels-emissions
                                                                                                                rate obtained w/subuierged
                                                                                                                fill (  1.5 psia. >5Z head
                                                                                                                  ace reactivity) >1000
                                                                                                                   - - - •   * •-
                                                                                                                                                 apuue i eact t vi \.y ) " luuu
                                                                                                                                                 barrels, 1.5 psla-ll psia
                                                                                                                                                 head space reactivity of 52-
                                                                                                                                                 floating roof >1000 barrels,
                                                                                                                                                 ^ 11 psia, ^531 head  space
                                                                                                                                                 reactivity - floating root
                                                                                                                                                 and same emissions  as 11 psia
                                                                                                                                Existing
                                                                         Hydrocarbon compounds
                                                                         from polymer synthesis
                                                                         process emission source
                                                                         shall be bunted at 1300"F
                                                                         for 0.3, seconds or longer.
                                                                         Slowdown emissions to be
                                                                         burned in smokeless flure
                                                                         or equivalent.
                                                                                                                                                 fixed roof, float ing roof

                                                                                                                                                 >40,000 gals floating roof
                                                                                                                                                 for psia or less.
                                                                                                                                                 New

                                                                                                                                                 >40,000 gal-pressure
                                                                                                                                                 tank or vapor recovery
                                                                                                                                                 >250 gal.-submerged fill
                                                                                                                                                 or pressure tank or vapor
                                                                                                                                                 recovery.
                                                                                                                                <1000 gal-exempt if under-
                                                                                                                                ground 2/offset fill  line.

-------
_. - ,
State
l)e liiware
Florida
Georgia
. 	
A()CKl
45
5
49
50
2
56
58
- , TAIil.E A-4. (Continued)
Oil-Water Catalytic Vapor
Load ing Hacks Separat ion Kegenerators tlluwdowa Storage
None None None None
•HI None
No person shall store,
puuip , handle , process,
load , unload or use In
tlou volatile organic
solvents wt thout applying
known and existing vapor
emission control devi ces
aty and ordered by the
Department
None None None None None
                 Hawaii
                                     60
                                             None
 I
u>
                 Illinois
                                     65
                                     67
                                     70
                                     73
                                     67
                                     80
                                     HI
ti5% control of splash
top loading for units
with a throughput of
40,000 gallons u day
if more than 8 pounds
are emitted.
                                                      1  and  all  New
Sources
                                             For  racks  handling
                                             40,000  gallons  a  day  or
                                             wore , a vapor  recovery
                                             system  lit  good  working
                                             order  is requf red.
                             >200 g volatile
                             organic compound-
                             vapor loss control
                             device.

                             New

                             All sources after
                             1/1/75
Existjng

B5Z control of emis-
sions If unit handles
200 gallons or more
of organic material
a day.
                             If unit handles 200
                             ga1Ions a day or more
                             of volatile organics,
                             units must be equipped
                             with a solid or floating
                             cover, a vapor recovery
                             system, or equivalent
                             method.
                                                                                                    Existing
                                                                                                                        All  sources  after
                                                                                                                        1/1/75
                                                                           Existing
100 ppui of equiv-    10 pput equivalent
alent methane.       methane or burning
                    in a smokeless flare.
                          Emissions must be   Slowdown must vent
                          burned in a direct- to a flap.
                          flame afterburner
                          or boiler.
>40,000g-pressure tank or
vapor recovery device

>250g-pyruianent submerged
fill or pressure lank or
vapor recovery.device

New

All sources after 1/1/75

|i x i a t ing

Floating roof or B52 vapor
recovery for tanks oi:
40.000 gallons or more
storing volatllea.
                                             Floating roof or vapor
                                             recovery for tanks of 40,000
                                             gallons or more storing vola-
                                             tile (2.5 psla or greater).

-------
State
Kiinsas

Kentucky
Louis lana
AQCKf Loading Hacks
% None
07
98
99

103 None
105
22 Existing
106
Oil Water Catalytic Vapor
Separation Regenerators DlowJown
None None Exist ing
<50 Ib/lu IIC or be
controlled by a
Sfuokelc-ss flare.
New
Same as existing
None None None
Existing None None
Storage
Existing
>40,000 gal + >3 psia must
have floating roof ;
40,000 gal i- >13 |jula
New
Same ati existing
None
Existing

oo
                 Maine
>^0,000 g/d throughput
(30 day avy.) und filling
>200g cuaculucrs - vapor
collection and dlspouul
or equlvaluitl; or 952
submerged fill, of
bottom loading.

Huw

>20.000 &/4uy through-
put (30 day avg.)
filling >200g coiUaliiers-
vapor collection and dis-
posal or equivalent, or
952 buhmergcd fill, or
hot toui load Ing.

None
      volatile
organic compound* -
vapor loss control
device or equivalent.

New

>200 g Reid v.p. >0.5u-
vapor load control device
or equivalent.
                                                                                                                                                     >50,000g-preasuce  tank
                                                                                                                                                     or vupor  loaa  control
                                                                                                                                                     device.   >250g-dubmurged
                                                                                                                                                     fill  pipe or vapor
                                                                                                                                                     recovery  device.

                                                                                                                                                     New
                                                                                                                                                               ri;£itJure tank or
                                                                                                                                                     vapor  lostj  control device.
                                                                                                                                                     >250g  -  uaiuu  as  exJsllng.
                                                                            None
                                                                                                      None
                                                                                                                        None
                                                                                                                                                    None
                 Mary land
                                     115
                                     116
                                                                                                      Monti
                 Mussachusetts
                                      /i 2
                                     119
K x i s t i n g

>20,000 g/d throughput
(1,300 annual) handling
1.5 pa Ia or greater -
vapor recovery, vapor
tight fittings .
                                                                            None
                                                                                                                        None
                                                                         Existing

                                                                         >40,000 w/1.5-11  paia v.p.
                                                                         vupor  loss  control  device
                                                                         or  equivalent   40,000 w/U
                                                                         pula vp or  greater-vapor
                                                                         loss control device or
                                                                         etjul valent.

-------
Sratc
Michigan
Minnesota



Mississippi
Missouri
Montana
Oil -Water Catalytic
AlJCKtf l.mi.liuii Hacks Separation Iteyeneratora
122 None None None
129 None None None
131
132

5 None None None
IB
70 None None None
1 40 None Ex 1 a t ing None
Vapor
None None
None Existing

Flouting roof or
65,000 gala or mo
storing volutlles
psiu or greater).
None None
None None
None Existing




vapor
re
(2.5



                             Unitu >200 g/d of
                             petroleum product
                             must have vapor tight
                             fixed roof, floating
1
U)
Nebraska
New tlaiuuslil re
New Jersey
New Mexico




146
121
43
45
14
153



None
None
None
Existing
None
New
f
and disposed system.
None Nona None
None None None
None None None
Existing None Existing

equivalent
New
Lem Units handling >600 gal/d
or equivalent.
                             of hydrocarbons or refiner-
                             ies with  10.000 bpd capa-
                             city uins t have coup 1 e t e
                             unit enclosing liquid con-
                             tents or equivalent.
Fixed roof, flouting roof
or vapor recovery system
if 65,000 gals or more
above 2.5 psla.  Kefiner-
ies processing less than
7000 bpd crude oil charge
are exempt.

None
Pressure vessel or equiv-
alent if 250,000 gals or
more and above 11.0 psla.
Floating roof or vapor
recovery system If 250,000
ga Is or more and between
3.0 and 11.0 psla.

New

Pressure vessel or equiva-
lent If 65,000 gals or
more and above 11.0 psla.
Floating roof or vapor
recovery system if 65.000
gals or more and between
1.5 psia and 11.0 psla.

-------
TABLE £-4, {Continued}

State
New York



North Dakota




AQUtf
•<.•!
158
161
162
112



Oil-Water
Loading Racks Separation
None None



Existing None
None

New
Catalytic Vapor
Kegcnerators blowilown
None None



None Existing
Host be burned by
giuokeless flare.


Storage
None



Exi sting
None

New
>
o
                     103
                     124
                     174
Ok lalioina
                      17
                      22
                     186
                     188
                              New loading facilities
                              handling 20.000 gals per
                              day or more must be equip-
                              ped with submerged fill or
                              other vapor emission con-
                              trol systems.

                              I'riQrity I KeKlons and all Mew Sources
                              For racks handling 40.000
                              galIons a day or more of
                              vulatlies, a vapor
                              re c ov e r y s y s t eiu.
                              New

                              >40.000 g/d-vapor
                              collection and disposal
                              or bottom loading, vapor
                              tight seal between adapt-
                              or and hatch, or vapor
                              tight connection if
                              loading other than
                              through hatches.
For units handling 200
gallons a day or otore
of orgunlcs-equipped
with a solid or
floating cover, a
vupor recovery system,
or equivalent method.
None

New

>200 g/il volatile
organic material-
vapor loss control
device required or
equivalent.
Existing

Must be burned by
siuokel ess flare.
                                                                                     None
Must be burned by
tiuoke Less f 1 a re.
                                                                        Storage  tanks greater
                                                                        than 63,000 gals con-
                                                                        taining  volatile organics
                                                                        must be  equipped with
                                                                        floating roof or equiv-
                                                                        alent .
floating roof or vapor
recovery for tanks of
65,000 gallons or more
storing volatile^ (l.S
psla or greater).
Existing

None

New

>40,000g-pressure
tank or vapor loss con-
trol device or equivalent.

>2500-suboierged fill or
vapor recovery
Oregon
                              None
                                                           None
                                                                                     None

-------
State
Pennsylvania




Tennessee

Texas




AQCK
45
178
197


7
18
22
106
212
214
216
217
Loading Hacks
Existing

>20,000 gal/day-vapor
recovery

None

Existing

>20,UOOg/d throughput
(avg. 30 day) - vapor
that aggregate partial
Oil-Water Catalytic
Separation Kegeneratora
Existing None

>2UO gal/day-floating


None None

Existing None

>200 gd volatile
organic compounds

Vapor
Ulowdown
None




None

Existing

Uurn at 1300'P In
smokeless flare or
tor.
- Storage
Existing

>40.00O gal + >1.5
>40,000 gal + >11.0
psla vapor recovery.
None

Existing

>25,000|5-pressure tar
or vapor loss control
>1000g-subuierged fill
pressure of emissions
is  1.5 psla; vapor
tIght seal between
adaptor and hatch; or
vapor tIght connections
if hatches aren't used.
Utah
Virginia
Washington
219
220
223
228
229
None
None
None
None
None
None
None
None
None
None
None
None
                                                                                                                                     prtibtiure tank or
                                                                                                                                     recovery .
                                                                                                                                     Crude oil and coiuleusale
                                                                                                                                     storage lixuuipL.
                                                                                                                                     > 6 5.OOO gallons ca|Kicity
                                                                                                                                     of gasoline or uny other
                                                                                                                                     petroleum distillate
                                                                                                                                                 or
                                                                                                                                     >6,000 gal lottn capacity,
                                                                                                                                     any organic 1 Iqiild or
                                                                                                                                     solvent
                                                                                                                                     >1.5 psl Kuld must have
                                                                                                                                     f loai:lng roof , vapor
                                                                                                                                     recovery or equivalent.
West Virginia
                    103
                              None
                                                                                                         None
                                                                                                                                     None

-------
                State
                                  AQCK0
                                            Loading  hacks
                                   129
Oil-Water
Separation
 Catalytic
Kegenerators
                                                                                                                      Vapor
                                                                                                                     Ulowdown
                                                                                                                                                 Storage
                                                                                                                                                 Exial-iii

                                                                                                                                                 None
             Wyoming
                                                                         Any  new  oil-water
                                                                         separator  chat  pro-
                                                                         cuasea 200 gallonu
                                                                         a  Jay must control
                                                                         euilutiioaB  by  B5Z.

                                                                         None
                                              Floating roof or vapor
                                              recovery for tanks of
                                              40,000 gallons or more
                                              storing volatlles (l.S
                                              puia or greater).

                                              None
                                   242
 I
4>
ro

-------
   APPENDIX B

  Study Results
Forms 1 Through 6
      B-l

-------
           FORM 1





Baseline Energy Consumption
            B-2

-------
74
HO
85
                      FORM 1

           BASELINE ENERGY CONSUMPTION
                 Purchased Fuels
Industry:
Sub'sector
Year:
Region:
Data Type: 1-BEC
Page 1 of 18
Petroleum Refining
N.A.
1974, 1930, 1985
1-Northeast
1
10C 11 tu
Physical
Units
i
10° litu
Physical
Units
10C Btu
Physical
Units
Coal ;
	
1
0.831
x 106
34.6
MTONS
3.020
x 106
126
MTONS
Oil
	
i
21.594
x 106
3,442
MBBLS
88.960
x 106
14,180
MBBLS
Gas
	
	
2.886
x 106
2,800
MMCF
i
	
Elec.
	
	
1.322
x 106
387
MMKWh
4.804
x 10G
1,406
MMKWh
LPG
	
	
0.492
x 106
123
MBBLS
1.788
x 106
447
MBBLS
Steam
	
	
1.234
x 106
1,028
MMlbs
4.484
x 106
3,736
MMlbs
                  Self-Generated Fuels
Elec.
	
	
0.114
x 1.0 6
33.4
MMKWh
0.414
x 106
121.4
MMKWh
Refinery
Gas
	
	
18.010
x 106
18,192
MMCF
65.448
x 106
66,110
MMCF
Catalytic
Coke
	
	
7.214
x 106
239
MTONS
26.216
x 106
869
MTONS

-------
74
80
85
                       FORM 1

            BASELINE ENERGY CONSUMPTION
                  Purchased Fuels
Industry:
Subsector:
Year:
Region:
Data Type:  i-BEC
Page 2 of 18
Petroleum Refining
N.A.
1974, 1980,  1985
2—Mid-Atlantic
\
10 G 11 tu
Physical
Units
!
10° Btu
Physical
Units
106 Btu
Physical
Units
Coal
4.204
x 106
175
MTONS
I
5.608
x 10G
233.5
MTONS
6.163
x 106
256.6
MTONS
Oil
94.586
x 106
15,077
MBBLS
|
145.646
x 106
23,217
MBBLS
181.459
x 10 6
28,926
MBBLS
Gas
29.187
x 106
28,309
MMCF
19.467
x 10 6
18,882
MMCF
	
	
Elec.
6.684
x 106
1,959
MMKWh
8.916
x 106
2,613
MMKWh
9.799
x 106
2,872
MMKWh
LPG
2.487
x 106
620
MBBLS
3.318
x 106
827
MBBLS
3.646
x 106
909
MBBLS
Steam
6.239
x 106
5,199
MMlbs
8.323
x 106
6,935
MMlbs
9.147
x 106
7,622
MMlbs
                   Self-Generated Fuels
Elec.
0.575
x 10 6
168
MMKWh
0.767
x 106
225
MMKWh
0.843
x 106
247
MMKWh
Refinery
Gas
91.056
x 106
91,976
MMCF
121.469
x 106
122,696
MMCF
133.494
x 106
134,843
MMCF
Catalytic
Coke
36.475
x 106
1,211
MTONS
48.658
x 106
1,615
MTONS
53.475
x 106
1,775
MTONS

-------
74
80
85
                       FORM  1

            BASELINE ENERGY  CONSUMPTION
                  Purchased  Fuels
Industry:   Petroleum Refining
Subsector:  N.A.
Year:       1974,  1980, 1985
Region :     3-South Atlantic
Data Type :  1-BEC
Page 3 of 18
!

106 Btu
Physical
Units

1
10C Btu

Physical
Units
10r> Utu
Physical
Units
Coal
0.5525
x 106
23
MTONS

i
1.695
x 106
70.56
MTONS
2.078
x 106
86.51
MTONS
Oil
10.204
x 106
1,671
MBBLS
I

36.267
x 106
5,934
MBBLS
50.546
x 106
8,270
MBBLS
Gas
3.234
x 10 6
3,137
MMCF


4.961
x 106
4,812
MMCF
	
	

Elec.
2.136
x 106
626
MMKWh


6.553
x 106
1,921
MMKWh
8.034
x 106
2,355
MMKWh
LPG
0.281
x 106
70
MBBLS


0.86-2
x 106
215
MBBLS
1.057
x 106
264
MBBLS
Steam
7.060
x 106
5,883
MMlbs


21.660
x 106
18,049
MMlbs
26.555
x 10 6
22,128
MMlbs
                   Self-Generated Fuels
Elec.
0.184
x 10G
54
MMKWh
0.564
x 106
165
MMKWll
0.691
x 106
202
MMKWh
Refinery
Gas
24.157
x 106
24,401
MMCF
74.114
x 106
74,862
MMCF
90.864
x 106
91,781
MMCF
Catalytic
Coke
12.831
x 106
426
MTONS
39.366
x 106
1,307
MTONS
48.263
x 106
1,602
MTONS

-------
74
80
85
                       FORM  1

            BASELINE ENERGY  CONSUMPTION
                  Purchased Fuels
Industry:
Subsector:
Year:
Region:
Data Type:
Page 4 of 18
Petroleum Refining
N.A.
1974, 1980, 1985
4-East North Central
1-BEC


106 litu
Physical
Units
10G Btu
Physical
Units
10C Btu

Physical
Units
Coal
0.4083
x 106
17
MTONS
0.4691
x 106
19.5
MTONS
0.4836
x 10
20.1
MTONS
Oil
100.66
x 106
16,054
MBBLS
137.119
x 106
21,869
MBBLS
163.496
A
x 106
26,076
MBBLS
Gas
37.356
x 106
36,233
MMCF
21.461
x 106
20,816
MMCF




Elec.
13.020
x 106
3,816
MMKWh
14.960
x 106
4,385
MMKWh
15.424
x 106
4,521
MMKWh
LPG
6.747
x 106
1,682
MBBLS
7.752
x 106
1,933
MBBLS
7.992
x 106
1,993
MBBLS
Steam




	






                   Self-Generated Fuels
Elec.
1.120
x 106
328
MMKWh
1.287
x 106
377
MMKWh
1.327
x 106
389
MMKWh
Refinery
Gas
176.090
x 106
177,869
MMCF
202.327
x 106
204,371
MMCF
208.599
x 106
210,707
MMCF
Catalytic
Coke
78.643
x 106
2,611
MTONS
90.361
x 106
3,000
MTONS
93.162
x 106
3,093
MTONS

-------
74
80
                       FORM  1

            BASELINE ENERGY  CONSUMPTION
85 '
                  Purchased Fuels
Industry:
Subsector:
Year:
Region:
Data Type:
Page 5 of 18
Petroleum Refining
N.A.
1974, 1980,  1985
5-East South Central
1-BEC
1
10G 11 tu
Physical
Units
1
10° Btu
Physical
Units
10° lltu
Physical
Units
Coal ;
	
I
	
	
	
	
Oil
10.462
x 106
1,672
MBBLS
}
43.827
x 106
7,004
MBBLS
79.202
x 10G
12,658
MBBLS
Gas
31.470
x 106
30,524
MMCF
26.325
x 106
25,533
MMCF
1
	
Elec.
2.365
x 106
693
MMKWh
3.957
x 106
1,159
MMKWh
4.467
x 106
1,309
MMKWh
LPG
l'.'336
x 10G
333
MBBLS
2.235
x 106
557
MBBLS
2.523
x 106
629
MBBLS
Steam
1.778
x 106
1,483
MMlbs
2.975
x 106
2,470
MMlbs
3.359
x 106
2,799
MMlbs
                   Self-Generated Fuels
Elec.
0.203
x 106
60
MMKWh
0.340
x 106
99.7
MMKWh
0.384
x 106
112.6
MMKWh
Refinery
Gas
43.195
x 106
43,631
MMCF
72.265
x lu6
72,995
MMCF
81.587
x 106
82,411
MMCF
Catalytic
Coke
10.934
x 106
363
MTONS
18.293
x 106
607
MTONS
20.653
x 106
685
MTONS

-------
74
80
85
                       FORM 1
            BASELINE ENERGY CONSUMPTION
                  Purchased Fuels
Industry:
Subsector
Year:
Region:
Data Type: . 1-BEC
Page 6  of 18
Petroleum Refining
N.A.
1974, 1980,  1985
6-West North Central
!
10G btu
Physical
Units
i
106 Btu
Physical
Units
10G btu
Physical
Units
Coa 1 |

	
	
	
	
	
Oil
16.692
x 106
2,655
MBBLS
47.613
x 106
7,573
MBBLS
73.71
x 106
11,724
MBBLS
Cas
40.492
x 106
39,371
MMCF
26.097
x 106
25,312
MMCF
	 ;
	
l£lec.
3.641
x 106
1,067
MMKWh
4.693
x 106
1,375
MMKWh
4.693
x 106
1,375
MMKWh
LPC
0.963
x 106
240
MBBLS
1.241
x 106.
309
MBBLS-
1.241
x 106
309
MBBLS
Steam
	
	
	
	
. 	
	
       Self-Generated Fuels
Elec.
0.313
x 106
91.8
MMKWh
0.404
x 106
118.3
MMKWh
0.404
x 106
118.2
MMKWh
Refinery
Gas
52.811
x 106
53,344
MMCF
68.074
x 106
68,760
MMCF
68.074
x 106
68,760
MMCF
Catalytic
Coke
20.692
xr 106
687
MTONS
26.672
x 106
886
MTONS
26.672
x 106
886
MTONS

-------
74
80
85
                       FORM 1

            BASELINE ENERGY CONSUMPTION
                  Purchased  Fuels
Industry:
Subsector:
Year:
Region:
Data Type:
Page 7 of 18
1
10G Btu
Physical
Units
i
106 litu
Physical
Units
106 Btu
Physical
Units
Coal :
i
i
	
	
	
	
Oil
33.826
x 106
5,658
MBBLS
i
577.310
x 106
96,572
MBBLS
L252.011
x 106
209,436
MBBLS
Gas
769.636
x 10G
746,495
MMCF
530.664
x 106
514,708
MMCF
— ;
—
Elec.
29.023
x 106
8,506
MMKWh
40.023
x 106
11,730
MMKWh
45.226
x 106
13,255
MMKWh
LPC
11.644
x 106
2,903
MBBLS
16.057
x 106
4,003
MBBLS
18.144
x 106
4,523
MBBLS
Steam
15.115
x 106
12,596
MMlbs
20.844
x lu6
17,370
MMlbs
23.554
x 10G
19,628
MMlbs
Petroleum Refining
N.A.
1974, 1980,  1985
7-West South Central
1-BEC
                   Self-Generated Fuels
Elec.
2.496
x 106
732
MMKWh
3.442
x 106
1,009
MMKWh
3.889
x 106
1,140
MMKWh
Refinery
Gas
437.203
x 106
441,619
MMCF
602.903
x 10G
608,993
MMCF
681.280
x 106
688,162
MMCF
Catalytic-
Coke
141.263
x 106
4,690
MTONS
194.802
x 106
6,468
MTONS
220.126
x 106
7,309
MTONS

-------
74
80
85
                       FORM 1

            BASELINE ENERGY CONSUMPTION
                  Purchased Fuels
Industry:
Subsector:
Year:
Region:
Data Type:
Page 8 of 18
1
10° Utu
Physical
Uaits
106 Btu
Physical
Units
10G Btu
Physical
Units
Coal
	
I
	
	 :
	
)
Oil
14.543
x 106
2,320
MBBLS
35.012
x 10G
5,585
MBBLS
53.391
x 106
8,495
MBBLS
Gas
31.716
x 106
30,762
MMCF
18.113
x 106
17,568
MMCF
	 ;
	
Elec.
2.740
x 106
803
MMKWh
3.184
x 106
933
MMKWh
3.200
x 106
938
MMKWh
LPG
2.042
x 106
509
MBBLS
2.373
x 106
591
MBBLS
2.385
x 106
594
MMKWh
Steam
	
	
	
	
	
	
Petroleum Refining
N.A.
1974, 1980, 1985
8-Mountain
1-BEC
                   Self-Generated Fuels
Elec.
0.236
x 106
69
MMKWh
0.274
x 106
80
MMKWh
0.275
x 106
80.4
MMKWh
Refinery
Gas
37.882
x 106
38,265
MMCF
44.019
x 106
44,464
MMCF
44.239
x 106
44,686
MMCF
Catalytic-
Coke
18.012
x 106
598
MTONS
20.930
x 106
695
. MTONS
21.035
x 106
698
MTONS

-------
80
85
                       FORM 1

            BASELINE ENERGY CONSUMPTION
                  Purchased  Fuels
Industry:
Subsector:
Year-
Region :
Data Type:
Page 9 of 18
Petroleum Refining
N.A.
1974, 1980, 1985
9-P.acific
1-BF.C
1
]0r< 11 tu
Physical
Units
!
10 6 ntu
Physical
Units
10f> Btu
Physical
Units
Coal
	
	
	
	
	
	
Oil
35.309
x 106
5,710
MBBLS
L60.280
x 106
25,921
MBBLS
113.764
x 10G
50,742
MBBLS
Gas
129.108
x 106
125,226
MMCF
103.609
x 106
100,494
MMCF
	
	
Elec.
19.216
x 106
5,632
MMKWh
30.842
x 106
9,039
MMKWh
36.671
x 106
10,747
MMKWh
LPG
14.006
x 106
3,492
MBBLS
22.480
x 106
5,605
MBBLS
26.729
x 106
6,664
MBBLS
Steam
12.632
x 106
10,527
MMlbs
20.274
x 106
16,896
MMlbs
24.106
x 106
20,089
MMlbs
                   Self-Generated Fuels
Elec.
1.653
x 106
484
MMKWh
2.652
x 106
777
MMKWIi
3.153
x 106
924
MMKWh
Ref inei-y
Gas
180.719
x 106
182,544
MMCF
290.054
x 106
292,983
MMCF
344.874
x 106
348,357
MMCF
Catalytic
Coke
55.120
x 106
1,830
MTONS
88.468
x 106
2,937
MTONS
105.188
x 106
3,492
MTONS

-------
      FORM 2
Baseline Production

-------
       FORM 2
BASELINE PRODUCTION
Industry:
Subsector:
Year:
Region:
Data Type:
Petroleum Refining
N.A.
1974, 1980, 1985
1-9
2-BP
Page 10 of 18  '

Units:  Crude Running,
        103 Barrels per Calendar Day

Production
1974
Production
1980
Growth
Rate
Production
1985
Growth
Rate
Census
Region
1
0
235
N.A.
854
263.4
Census
Region
1
1188
1585
33.4
1742
9.0
Census
Region
3
221
678
206.8
831
22.6
Census
Region
4
2060
2366
14.9
2438
3.1
Census
Region
437
731
67.3
825
12.9
Census
Region
6
644
830
28.9
830
0
Census
Region
7
5232
7215
37.9
8151
13.0
Census
Region
8
482
560
16.2
563
0.5
Census
Region
9
1869
3000
60.5
3566
. 18.9

-------
     FORM 3





Percent Coverage

-------
               FORM 3
           PERCENT COVERAGE

      INDUSTRY COVERAGE IN 1974

% COVERAGE OF FUEL USE IN 'THE PARENT

     2 OR 3 DIGIT INDUSTRY (291)
Industry:
Subsector:
Year:
Region:
Data Type:
Page 11 of
 Petroleum Refining
 N.A.
 1974
 1-9
 3-PC
18


COAL

100


OIL

100


GAS

100

ELECTRICITY
(PURCHASED)

100
LPG
STEAM
OTHER
(PURCHASED)
100
                                           ELECTRICITY
                                          SELF-GENERATED
                                                100
        REF. GAS
        CAT. COKE
          OTHER
           100
     COVERAGE OF PRODUCTION
                COVERAGE
                  100

-------
                FORM 4





Regulatory Scenario/Control Strategy Mix

-------
                 FORM 4.
REGULATORY SCENARIO/CONTROL  STRATEGY  MIX
Industry:  Petroleum  Refining
Year:      1974,  1980,  1985
Region:     1-9
Data Type:
Page 1  of 6

Regulatory
Scenario
1
2
3
4
Regulatory
Scenario
Parficulates SIP
(Existing Sources)
Particulates SIP
(New Sources)
Particulates NSPS
Particulates RACT
CONTROL STRATEGY MIX #
1
Multiple
Internal
Cyclones
(MIC)
MIC
MIC
MIC, ESP,
and a Wet
Scrubber
2
MIC plus
Electro-
static Pre-
cipitator
(ESP)
MIC plus
ESP
MIC plus
ESP

3
MIC plus a
Wet Scrubbei
MIC plus a
Wet Scrubbei
MIC plus a
Wet Scrubbei

4




5





-------
                 I'UKH H

REGULATORY SCENARIO/CONTROL STRATEGY MIX
Industry:
Year:
Region:
Data Type:
Page 2  of
Petroleum Refining
.1974, 1980,  1985
1-9
4-RSCS
6

Kejvilc'i Cory
Scenario

5




6




7




8



9


10



Regulatory
Scenario
S<>2 SI I' (Existing
Source)



St>2 SIP (New
Sources)



S02 NSPS




S0? RACT




SO., 0.7 wt.
% S Km; I


S02 0.3 wt.
7. S Fuel
CONTROL STRATEGY MIX #

1
Se ) ec t i ve Fue.
Blending;
Clans Unit


Se 1 ec t ive
Fuel 11 lend-
ing


Sol active
Fuel. Blend-
ing


Selective
Fuel Blend-
ing


Se lectlve
Fuel HI end-.
ing


Selective
Fuel Blend-
ing




•
2
1! lending plus
some Gas Oil
1IDS; Clans
Unit

Blending plus
some Gas Oil
IIDS; Claud
Unit

Blending plus
some Gas Oil
IIDS; Clan:;
lln i t

Blending plus
some Gas 01.1
1IDS; Glaus .
lln it:

Blending plus
some Gas Oil.
IMS; Claus
Unit

Blending plus
some Gas Oil
1IDS; Clau.'i
Unit


3
Bli.'iidjng plus
IlltS of FCC
Feed; Claus
Unit with Tail
Gas Treati.ng
Blending plus
11 DS of: FCC
Feed ; Glaus
Unit with Tail
Gas Treating
Blending plus
IIDS of FCC
Feed ; Glaus
Unit with Tail
Gas Treating
Blending plus
IIDS of FCC
Feed ; Claus
llni.t with Tal 1
Gas Treati.ng
Blending pins
III IS ol" FCC
Feed; Claus
Unit with Tail
Gas Treating
Blending plus
II US of FCC
Feed; Glaus
Unit with Tail
Gas Treating

ft
No. 3 plus Gas
Oil HDS



No. 3 plus Gas
Oil HDS



No. 3 plus Gas
Oil HDS



No. 3 plus Gas
Oil HDS



No. 3 plus Gas
Oil IIDS


No. 3 plus Gas
Oil HDS




5
Blending Gas Oil
IIDS, FCC Flue Gas
Scrubbing; Glaus
with Tail Gas
Treating
Blending Gas Oil
IIDS, FCC Flue Gas
Scrubbing; Claus
wi tli Tall Gas
Treat ing
Blending Gas Oil
HDS , FCC Flue Gas
Scrubbing; Claus
with Tail Gas
Treating
Blending Gas Oil
IIDS, FCC Flue Gas
Scrubbing; Claus
with Tail Gas
Treat ing
Blending Gas Oil
IIDS, FCC Flue Gas
Scrubbing; Claus
with Tail Gas
Treating
Blending Gas Oil
IIDS, FCC Flue Gas
Scrubbing; Clans
with Tail Gas
Treating

-------
                 FORM 4

REGULATORY SCENARIO/CONTROL  STRATEGY  MIX
Industry:
Year:
Region:
Data Type:
Page  3  of
Petroleum Refining
1974,  1980, 1985
1-9
4-RSCS
6

Regulatory
Scenario
11
12
13
14
Regulatory
Scenario
N0x SIP
(Existing Units)
N0x SIP
(New Units)
N0x NSPS
NOX RACT
CONTROL STRATEGY MIX #
1
Two State
Combustion
Two Stage
Combustion
Two Stage
Combustion
Two Stage
Combustion
2
Flue Gas
Recircula-
tion
Flue Gas
Recircula-
tion
Flue Gas
Recircula-
tion
Flue Gas
Recircula-
tion
3




4




5





-------
                           FORM 4
         REGULATORY  SCENARIO/CONTROL STRATEGY MIX
Industry: ' Petroleum  Refining
Year:      1974,  1980,  1985
Region:    1-9
Data Type: 4-RSCS
Page 4  of 6

Regulatory
Scenario

19





20





21






22





Regulatory
Scenario
Hydrocarbon SIP
(Existing Sources)




Hydrocarbon SIP
(New Sources)




Hydrocarbon NSPS






Hydrocarbon RACT






CONTROL STRATEGY MIX #
1

Slowdown
vented to
flares ;
Pressure
tanks

Slowdown
vented to
flares ;
Pressure
tanks

Floating
roof tanks,
Slowdown
vented to
flares ;
Pressure
tanks
2

No. 1, plus
floating
roof tanks
and vapor
recovery
Q\7C J-oinc
No. 1, plus
floating
roof tanks
and vapor
recovery
systems
No. 1, plus
vapor
recovery
systems



Floating roof tanks,
vapor recovery, pres-
sure tanks, blowdown to
flares, floating cover
on API separator, and
Afterburner or Boiler-
Incinerator on the FCUU
3

No. 2, plus
floating
cover or
API
separators

No. 2, plus
floating
cover or
API
separators

No. 2, plus
floating
cover or
API
separators









4

No. 3, plus
Afterburner
or Boiler-
Incinerator
on the FCCU

No. 3, plus
Afterburner
or Boiler-
Incinerator
on the FCCU

No. 3, plus
Afterburner
or Boiler-
Incinerator
on the FCCU









5



























o

-------
                 FORM  4
REGULATORY SCENARIO/CONTROL  STRATEGY MIX
Industry:  Petroleum Refining
Year:      1974,  1980, 1985
Region:    1-9
Data Type: 4-RSCS
Page 5  of 6

Regulatory
Scenario
23
24
25

Regulatory
Scenario
Produce Unleaded
Gasoline to Meet
Market Demand
Lead Phasedown to
<0.5 gin/gal of the
Total Pool by
10-1-79
Zero Lead in
Gasoline

CONTROL STRATEGY MIX #
1
Increase
Processing
Severity to
Improve
Octanes
Increase
Processing
Severity to
Improve
Octanes
Increase
Processing
Severity to
Improve
Octanes

2
Some sever-
ity increase,
plus the use
of a non-
lead
additive
Some sever-
ity increase
3lus the use
of a non-
lead
additive
Some sever-
ity increase
ilus the use
of a non-
lead
additive

3




4




5





-------
                 FORM 4

REGULATORY SCENARIO/CONTROL  STRATEGY MIX
Industry:
Year :
Region:
Data Type:
Page 6  of
Petroleum Refining
1974, 1980,  1985
1-9
4-USCS
6

Regulatory
Scenario
26
27
28
29
Regulatory
Scenario
Existing State
Uastewater
Treatment
Requirements
BPCTCA/BADT-
Federal Effluent
Limitations
BADT-Federal
Effluent
Lim I ta tions
BATEA-Federal
Effluent
Limitations
CONTROL STRATEGY MIX #
1
Sour '/later Stripping, API
Separators, Dissolved Air
Floatation, Equal l?ation
Haul it , Clarif icat: Ion,
Trickling Filters
Sour Water Stripping, API
Separators, Dissolved Air
Floatation , Equalization
Basin, Clarification,
Trickling Filter, Filtra-
tion, Reduction In Flow
Sour Water Stripping, API
Separators, Dissolved Air
Fluatat ion, Equalization
ISasin, Clarification,
Trickling Filter, Filtra-
tion. Reduction in Flow
Sour Water Stripping, API
Separators, Dissolved Air
Floatation, Equalization
Basin, Clarification,
Trickling Filter, Filtra-
tion, Carbon Adsorption,
Reduction in Flow
2
No. 1 wi th Un-
aerated Lagoons
Replacing Trick-
ling Filters
Mo. 1 with Un-
aerated Lagoons
Replacing Trick-
ling Filters
^
No. 1 with Un~
aerated Lagoons
Replacing Trick-
ling Filters
No. 1 with Un-
aerated Lagoons
Replacing Trick-
ling Filters
3
No. 2 with
Aeration Towers
Replacing Un-
aerated Lagoons
No. 2 with
Aeration Towers
Replacing Un-
aerated Lagoons
No. 2 with
Aeration Towers
Replacing Un-
aerated Lagoons
No. 2 with
Aeration Towers
Replacing Un-
aerated Lagoons
A
No. 3 with
Aerated Lagoons
Replacing Aera-
tion Towers
No. 3 with
Aerated Lagoons
Replacing Aera-
tion Towers
No. 3 with
Aerated Lagoons
Replacing Aera-
tion Towers
No. 3 with
Aerated Lagoons
Replacing Aera-
tion Towers
5
No. 4 with
Activated
Sludge. Re-
placing
Aerated
Lagoons
No. 'i with
Activated
Sludge Re-
placing
Aerated
Lagoons
No. 4 with
Activated
Sludge Re-
placing
Aerated
Lagoons
No. A with
Activated
Sludge Re-
placing
Aerated
Lagoons

-------
       FORM 5





Primary Energy Penalty

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    1
Data Type: 5-PEP
Page i  of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
There we
Control
Strategy
Mix
•e no refir
PURCHASED FUEL'S
Coal
eries ir
Oil
Regior
Natural
Gas
1 in 19
Elec.
74.
LPG

Steam

SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

-£.

-------
                         FORM 5
                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:     1
Data Type: 5-PEP
Page 2  of  189
                                 ALL UNITS ARE IN 103  Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1 >
2
3
1
2
3
^/



>


1
. 2
3
1
PURCHASED FUEL'S
Coal



Not app!


Does i

Does i

Oil



icable


ot sat:

ot satd

Natural
Gas






sfy this

sfy this

Elec.






regulat
.026
regulat
0.653
LPG






ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

Jb
0)

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    1
Data Type: 5-PEP
Page 3  of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1 >
2
3
1
2
•3
1
2
3
1










PURCHASED FUELS
Coal


Not Aj



Does i

Does i

Oil


plicab]



ot sat:

ot sat:

Natural
Gas


e



sfy this

sfy this

Elec.






regulat
.026
regulat
0.653
LPG






ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                         FORM 5
                PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    2
Data Type: 5-PEP
Page 4  of 189
                                 ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does r


Does r


Does t

Does r

Oil
ot sati


ot sati


ot sati

ot sati

Natural
Gas
sfy this


sfy this


sfy this

sfy this

Elec.
regulat
0.022
0.527
regulat
0.022
0.527
regulat
.022
regulat
0.549
LPG
Lon


ion


Lon

Lon

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

fb

-------
                        FORM 5

                PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    2
Data Type: 5-PEP
Page 5  of 189
                                ALL UNITS ARE  IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1


1
2
3
1
PURCHASED FUEL'S
Coal
Does i


Does i


Does

Does

Oil
lot sat:


lot sat


rot sat

lot sat

Natural
Gas
sfy this


sfy thit


sfy thli

sfy thl:

Elec.
regulat
0.022
0.527
regulat
0.022
0.527
regulat
0.022
regulat
0,549
LPG
ion


ion


ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

Jb
QO

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    2
Data Type: 5-PEP
Page 6   of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does i


Does i


Does i

Does i

Oil
ot sat:


lot sat:


iot sat:

lot sat:

Natural
Gas
sfy this


sfy this


.sfy this

sfy this

Elec.
regulat
0.022
0.527
regulat
0.022
0.527
regulat
0.022
regulat
0.549C
LPG
ion


ion


ion

ion

Steam

s








SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    3
Data Type: 5-PEP
Page 7  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does i

Does i
Does i

Does i
Does i

Does i

Oil
ot sat:

ot sat:
ot sat:

ot sat:
ot sat:

.ot sat:

Natural
Gas
sfy thit

sfy this
sfy this

sfy this
sfy this

sfy this

Elec.
regulat
0.026
regulat
regulat
0.026
.regulat
regulat
0.026
regulat
0.653
LPG
ion

ion
ion

ion
ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                        FORM  5

                PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    3
Data Type: 5-PEP
Page 8  of 189
                                 ALL UNITS ARE IN 10s Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does i

Does i
Does i

Does i
Does i

Does i

Oil
lot sat:

ot sat:
ot sat:

lot sat:
ot sat:

lot sat:

Natural
Gas
sfy this

sfy this
sfy this

sfy this
sfy this

sfy thit

Elec.
regulat
0.026
regulat
regulat
0.026
regulat
regulat
0.026
regulat
0.653
LPG
ion

ion
ion

ion
ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

GJ

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:       1985
Region:    3
Data Type: 5-PEP
Page 9  of 189
                                 ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does r

Does r
Does r

Does r
Does r

Does r

Oil
ot sati

ot sati
ot sati

ot sati
ot sati

ot sat]

Natural
Gas
sfy this

sfy this
sfy this

sfy this
sfy this

sfy this

Elec.
regulat
0.026
regulat
regulat
0.026
regulat
regulat
0.026
regulat
0.653
LPG
Lon

ion
ion

ion
ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

Co

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:       1974
Region:      A
Data Type: 5-PEP
Page 10  of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4 •
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUELS
Coal
Does r


Does r


Does r

Does r

Oil
ot sati


ot sati


ot sati

ot sati

Natural
Cas
sfy this


s f y th i s


sfy this

sfy this

Elec.
regulat
0.0258
0.625
regulat
0.0258
0.625
regulat
0.0258
regulat
0.651
LPG
Lon


ion


ion

Lon
•
Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

0)
Ol

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:     A
Data Type: 5-PEP
Page 11  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUELS
Coal
Does r


Does r


Does r

Does i

Oil
ot sati


ot sati


ot sati

ot sati

Natural
Gas
sfy this


sfy this


sfy this

sfy this

Elec.
regulat
0.0258
0.625
regulat
0.0258
0.625
regulat
0.0258
regulat
0.6510
LPG
Lon


Lon


Lon

Lon

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas
•
Catalytic
Coke


-------
                        FORM 5

                PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    4
Data Type: 5-PEP
Page 12  of 189
                                ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does i


Does i


Does i

Does

Oil
tot sat:


iot sat:


lot sat:

iot sat:

Natural
Gas
sfy this


sfy this


sfy this

.sfy this

Elec.
regulat
0.0258
0.625
regulat
0.0258
0.625
regulat
0.0258
regulat
0.651
LPG
ion


ion


ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

0)

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:       1974
Region:     5
Data Type: 5-PEP
Page 13 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUELS
Coal
Does r


Does i

Does r
Does r

Does r

Oil
ot sati


ot sati

ot sati
ot sati

ot sati

Natural
Gas
sfy this


sfy this

sfy this
sfy this

sfy this

Elec.
regulat
0.0176
0.425
regulat
0.0176
regulat
regulat
0.0176
regulat
0.443
LPC
Lon


Lon

Lon
Lon

Lon

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                        FORM 5
                PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    5
Data Type: 5-PEP
Page 14 of  189
                                ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does i


Does i

Does i
Does i

Does

Oil
lot sat:


tot sat:

tot sat:
lot sat:

lot sat:

Natural
Gas
sfy this


sfy this

,sJ:y this
.•sfy this

.sfy this

Elec.
regulat
0.017(
0.425
regulat
0.017*
regulat
regulat
0.017(
regulat
0.443
LPG
ion


ion

ion
ion

ion

Steam
*









SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

GO

-------
                         FORM 5

                 PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    5
Data Type: 5-PEP
Page 15 of 189
                                 ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does r


Does i

Does r
Does i

Does i

Oil
ot sati


ot sati

ot sati
ot sati

ot sati

Natural
Gas
sfy this


sfy this

sfy this
sfy this

sfy this

Elec.
regulat
0.0176
0.425
regulat
. 0.0176
regulat
regulat
0.0176
regulat
0.443
LPG
ton


Lon

Lon
Lon

Lon

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

GO

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:     6
Data Type: 5-PEP
Page 16  of  189
                ALL UNITS ARE IN  103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does i


Does T

Does i
Does i

Does i

Oil
ot sat:


ot sat:

lot sat:
ict sat:

lot sat:

Natural
Gas
sfy this


sfy this

sfy this
sfy this

sfy this

Elec.
regulat
0.0253
0.612
regulat
0.0252
regulat
regulat
0.025:
regulat
0.637
LPG
ion


ion

ion .
ion

ion

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                        FORM 5

                PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:     6
Data Type: 5-PEP
Page I?  of 189
                                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3
'

4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does r


Does i

Does i
Does i

Does r

Oil
ot sati


ot sati

ot sat]
ot sat:

ot sat:

Natural
Gas
sfy this


sfy this

sfy this
sfy this

sfy this

Elec.
regulat
0.0253
0.612
regulat
0.0253
regulat
regulat
0.0253
regulat
0.637
LPG
Lon


ion

ion
ion

Lon

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

-C
o

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:     6
Data Type: 5-PEP
Page 18  of  189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does r


Does r

Does r
Does r

Does r

Oil
ot sati


ot sati

ot sati
ot sati

ot sati

Natural
Gas
sfy this


sfy this

sfy this
sfy this

sfy this

Elec.
regulat
0.0253
0.612
regulat
0.0253
regulat
regulat
0.0253
regulat
0.637
LPG
Lon


Lon

Lon
Lon

Lon

Steam










SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:-  Petroleum Refining
Year:      1974
Region:    1
Data Type: 5-PEP
Page xg  of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
.3
1
PURCHASED FUEL'S
Coal
Does not
—
—
Does not
'
—
Does not
—
—

Oil
satisi
—
—
satisi
—
—
satisJ
—
—

Natural
Gas
y this i
—
—
y this i
—
—
y this r
—
—

Elec.
egulatio
0.0170
0.411
equlatio
0.0170
0.411
egulatio
0.0244
0.590
0.614
LPG
i
—
—
i
—
—
i

—

Steam

—
—

—
—

—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    7
Data Type: 5-PEP
Page 20 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does no
—
Does no
Does no
—
Does no
Does no
—
Does no

Oil
: satis
—
: satis
: satis
—
: satis
: satis
—
: satis

Natural
Gas
:y this
—
:y this
:y this :
. —
:y this
:y this :
—
:y this :

Elec.
•egulatic
0.0244
•egulatic
•egulatic
0.0244
•egulatic
egulatic
0.0244
•egulatic
0.614
LPG
n
—
>n
n
—
n
n
—
n

Steam

—


—


—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-t.
U)

-------
                        FORM  5

                PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    7
Data Type: 5-PEP
Page 21 of 189
                                ALL UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does no
—
Does no
Does no
—
Does no
Does no
—
Does no

Oil
t satis
—
t satis
: satis
—
: satis
t satis
—
t satis

Natural
Gas
:y this
—
fy this
:y this
—
:y this
:y this
—
:y this

Elec.
'egulatii
0.0244
'egulati(
••egulatic
0.0244
"egulatic
:egulati<
.0.0244
•egulati<
0.614
LPG
>n
—
in
in
—
in
>n
—
m

Steam

—


—


—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-IT

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    3
Data Type: 5-PEP
Page 22  of 139
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does no
—
—
Does no
—
—
Does no
—
Does no

Oil
: satis
—
—
: satis
—
—
: satis
—
: satis

Natural
Gas
:y this :
—
—
'y this :
—
—
:y this :
—
:y this :

Elec.
egulatic
0.0191
0.463
egulatic
0.0191
0.463
egulatic
0.0191
•egulatic
0.482
LPG
n
—
—
n
—
—
n
—
n

Steam

—
—

—
—

—

s
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
*
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    8
Data Type: 5-PEP
Page 23 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
' 1
2
3
1
2
3
' 1
2
3
1
PURCHASED FUEL'S
Coal
Does no
—
—
Does no
—
Does no
Does no
—
Does no

Oil
: satis
—
—
: satis
—
: satis
: satis
—
: satis

Natural
Gas
:y this :
—
—
:y this -
—
:y this
:y this :
—
:y this :

Elec.
egulatic
0.0191
0.463
egulatic
0.0191
•egulatic
egulatic
0.0191
•egulatic
0.482
LPG
n
—
—
n
—
n
n
—
n

Steam

—
—

—


—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:       1985
Region:    8
Data Type: 5-PEP
Page 24  of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does nol
—
—
Does nol
—
Does nol
Does not
—
Does nol

Oil
satisi
—
—
satis
—
satisi
satisi
—
satisi

Natural
Gas
y this i
—
—
y this i
—
y this i
y this r
—
y this r

Elec.
egulatic
0.0191
0.463
egulatio
0.0191
egulatio
egulatio
0.0191
egulatio
0.482
LPG
n
—
—
n
—
n
a
—
n

Steam

—
—

—


—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    9
Data Type: 5-PEP
Page 25  of 139
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUELS
Coal
Does no
—
Does no
Does no
—
Does no
Does no
—
Does no

Oil
: satis
—
: satis
: satis
—
: satis
: satis
—
: satis

Natural
Gas
:y this
—
:y this
:y this :
—
:y this
:y this :
—
:y this

Elec.
•egulatic
0.0144
egulatic
•egulatic
0.0144
•egulatic
•egulatic
0.0177
egulatic
0.447
LPG
n
—
n
n
—
n
n
—
n

Steam

—


—





SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5

                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1930
Region:    9
Data Type: 5-PEP
Page 26 of 189
                                 ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUEL'S
Coal
Does nc
—
Does nc
Does nc
—
Does nc
Does nc
—
Does nc

Oil
t satis
—
t satis
t satis
—
t satis
t satis
—
t satis

Natural
Gas
fy this
—
fy this
fy this
—
fy this
fy this
—
fy this

Elec.
regulati
0.01-44
regulati
regulati
0.0144
regulati
regulati
0.0177
regulati
0.447
LPG
m
—
)n
m
—
m
)n
—
Dn

Steam

—


—


—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-O

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:     .1985
Region:    9
Data Type: 5-PEP
Page 27 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
1


2


3


4
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1
PURCHASED FUELS
Coal
Does no
—
Does no
Does no
—
Does no
Does no
—
Does no

Oil
t satis
—
t satis
t satis

t satis
t satis
—
t satis

Natural
Gas
fy this
—
fy this
Ey this
—
fy this
fy this
—
fy this

Elec.
regulati
0.0144
regulati
regulati
0.0144
regulati
regulati
0.0177
regulati
0.447
LPG
>n
—
>n
)n
—
m
>n
—
jn '

Steam

—


—


—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                   FORM 5
           PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  1
Data Type: 5-PEP
Page 28 of 189
                           ALL  UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 '
2
3
4
5 .
1
2
3
4
5 .
1 >
2
3
4
5
1 ^
2
3
4
5












>




,


PURCHASED FUELS
Coal


There u




There v




There v




There v


Oil


ere no




ere no




ere no




ere no


Natural
Gas


ref ineri




ref ineri




ref ineri




ref ineri


Elec.


is in Re




ss in Re




ss in Re




as in Re


LPG


;ion 1 ii




>ion I ii




jion 1 ii




^ion 1 i


Steam


i 1974.




i 1974.




. 1974.




i 1974.


SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

01

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  1
Data Type: 5-PEP
Page 29 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 ")
2
3 ?
4
5 J
n
2
3
4
5j
PURCHASED FUELS
Coal


There .w




There w


Oil


ire no




jre no


Natural
Gas


•ef inerii




•ef inerii


Elec.


is in Re}




:s in Re}


LPG


ion 1 ir




ion 1 ir


Steam


1974.




1974.

s.
SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                    FORM 5

            PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  1
Data Type: 5-PEP
Page 30 of 189
                            ALL UNITS ARE IN 103 Btu/bbl. Crude  Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
1 ^
2
3 J
4
5
PURCHASED FUELS
Coal
	
—
—
—
—
—
—
—
—
—
	
—
—
—
—

Not a

—
—
Oil
6.25
14.86
22.00
32.52
16.51
6.25
14.86
22.00
32.52
16.51
6.25
14.86
22.0
32.52
16.51

jplicab

32.52
16.51
Natural
Gas
__
—
—
—
—
—
—
—
—
—
	
—
—
—
—

Le

—
—
Elec.
0.736
1.266
1.529
2.208
1.873
0.736
1.266
1.529
2.208
1.873
0.736
1.266
1.529
2.208
1.873



2.208
1.873
LPG
	
—
—
—
—
—
—
—
—
—
—
—
—
—
—



—
—
Steam
	
—
—
—
—
—
—
—
—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
d
Go

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region: 1
Data Type: 5-PEP
Page 31 of   189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9



10



Control
Strategy
Mix
1 >
11
4
5
IV
3 J
4
5
PURCHASED FUELS
Coal

Not a
—
—
Not a

—

Oil

pplicab
46.455
25.28
pplicab

52.9
37.815
Natural
Gas

le
—
—
le

•

Elec.


5.26
5.17


6.735
6.865
LPG


—
—


—

Steam


—
—


—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  1
Data Type: 5-PEP
Page 32 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 -|
2
3 J
4
5
1 1
2
3 J
4
5
1
2
3
4
5
1 ^
2
3 J
4
5
PURCHASED FUELS
Coal

Does

—
—

Does

—
—
	
—
—
—
—

Not a

—
—
Oil

lot sat

24.318
16.293

lot sat

30.620
19.799
6.25
14.86
22.0
32.52
16.51

pplicab

32.52
16.51
Natural
Gas

Lsfy thi

—
—

isfy thi

—
—
—
—
—
—
—

Le

—
—
Elec.

j regula

2.764
2.730

j regula

3.472
3.426
0.736
1.266
1.529
2.208
1.873



2.208
1.873
LPG

:ion .

—
—

ion.

—
—
—
—
—
—
—



—
—
Steam



—
—



—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                   FORM  5

           PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  1
Data Type: 5-PEP
Page 33 of 189
                           ALL  UNITS  ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 ^
2
3 J
4
5
1 -)
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

>plicab

46.455
25.28

>plicab

52.9
37.815
Natural
Gas

.e

—
—

.e

—

Elec.



5.26
5.17



6.735
6.865
LPG



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
— '
Catalytic
Coke
—
0|

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:
Year: 1974
Region:   2
Data Type:
Page 34  of
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged
Petroleum Refining

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 i
2 f
3 J
4
5
1 1
2
3
4
5 J
1
2
3
4
5
1 >j
2 1
3 J
4
5
PURCHASED FUEL'S
Coal

Does

—
—


Not a


	
—
—
—
—

Not i

—
—
Oil

lot sat

4.622
2.567


pplicab


1.250
2.972
4.400
6.504
3.301

pplicab

6.504
3.301
Natural
Gas

Lsfy thi

—
—


Le


—
--
—
—
—

le

—
—
Elec.

; regula

0.336
0.293





0.147
0.253
0.306
0.442
0.375



0.442
0.375
LPG

:ion.

—
—





—
—
—
—
—



--
—
Steam



—
—





—
—
—
—
—



— .
—
5-PEP
189
harge
i
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                    FORM 5
            PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region: 2
Data Type: 5-PEP
Page 35 of 189
                            ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 1
2
3 J.
4
5
1 1
2
3 J
4 .
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

Dplicab

9.291
5.056

pplicab

10.58
7.563
Natural
Gas

Le

—
—

le

—

Elec.



1.052
1.034



1.347
1.373
LPG



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
CO

-------
                   FORM  5
           PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  igso
Region:  2
Data Type: 5-PEP
Page 36 of 189
                           ALL  UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
5



6




7




8




Control
Strategy
Mix
n
3 J
4
5
1 1
2
3 J
4
5
1
2
3
4
5
1 1
2
3 J
4
5
PURCHASED FUELS
Coal
Does

—
—

Does

—
—
—
—
—
—
—

Not a

—
—
Oil
lot sat

23.11
12.84

lot sat

11.88
8.45
6.25
14.86
22.0
32.52
16.51

pplicab

32.52
16.51
Natural
Gas
Lsfy thi

—
—

Lsfy thi

—
—
—
—
—
—
—

le

—
—
Elec.
; regula

1.681
1.466

; regula

1.052
0.965
0.736
1.266
1.529
2.208
1.873



2.208
1.873
LPG
:ion.

—
—

:ion.

—
—
—
—
—
—
—



—
—
Steam


—
—



—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
cn
-0

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region: 2
Data Type: 5-PEP
Page 37 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged
,
Regulatory
Scenario
9




10




Control
Strategy
Mix
1 "|
2
3 J
4
5
! x
2 i
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

>plicab

46.455
25.28

>plicab

52.9
37.8.15
Natural
Gas

Le

—
—

.e

—

Elec.



5.26
5.17



6.735
6.865
LPG



—
—



—

Steam



--
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: _1985
Region:  2
Data Type: 5-PEP
Page 38 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
5




6


7




8



Control
Strategy
Mix
1 ^
2
3 J
4
5
1)
4
5
1
2
3
4
5
1 > .
2 )
3 J
4
5
PURCHASED FUELS
Coal

Does

—
—
Does
—
—
	
—
—
—
—

Not £
—
—
Oil

not sat

22.18
12.47
not sat
20.13
11.67
6.25
14.86
22.0
32.52
16.51

pplicab
32.52
16.51
Natural
Gas

Lsfy thi

—
—
isfy thi
—
—
	
—
—
—
—

le
—
—
Elec.

> regula

1.629
1.430
3 regula
1.514
1.337
0.736
1.266
1.529
2.208
1.873


2.208
1:873
LPG

:ion.

—
—
:ion.
—
—
—
—
—
—
—


—
—
Steam



—
—

—
—
—
—
—
—
—


—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1985
Region:   2
Data Type: 5-PEP
Page 39  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 "1
2
3 J
4
5
1 1
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

Dplicab

46.455
25.28

pplicab

52.9
37.815
Natural
Gas

.e

—
—

le

—

Elec.



5.26
5.17



6.735
6.865
LPG



—
—



—

Steam



—
— —



--

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1974
Region:  3
Data Type: 5-PEP
Page 40 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
s
j



6




1




8




Control
Strategy
Mix
1 ^
'}
3 J
4
.5
1 "1
2
3 1
4
5 J
1
2
3
4
5
l ,
2 S
3 J
4
5
PURCHASED FUELS
Coal

Does
—
—
—


Not £


	
—
—
—
—

Not £

—
—
Oil

not sat
2.038
3.260
2.202


pplicab


1.250
2.972
4.400
6.504
3.301

pplicab

6.504
3.301
Natural
Gas

isfy thi
—
—
—


le


—
—
—
—
—

le

—
—
Elec.

3 regula
0.187
0.373
0.369





0.147
0.253
0.306
0.442
0.375



0.442
0.375
LPG

:ion.
—
—
—





—
—
—
—
—



—
—
Steam


—
—
—
*




—
—
—
—
— —



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region: 3
Data Type: 5-PEP
Page 41 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 ^)
2
3 J
4
5
1 ~)
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

pplicab

9.291
5.056

pplicab

10.58
7.563
Natural
Gas

Le

—
—

le

—

Elec.



1.052
1.034



1.347
1.373
LPC



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas

Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1980
Region:  3
Data Type: 5-PEP
Page 42 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5



6



7




8




Control
Strategy
Mix
0
3
4
5
0
3 ^
4
5
1
2
3
4
5
1 >
2
3 J
4
5
PURCHASED FUELS
Coal
Does
—
—
—
Does
—
—
—
	
—
—
—
—

Not a

—
—
Oil
lot sat
13.43
24.57
14.92
lot sat
14.05
26.15
15.67
6.25
14.86
22.0
32.52
16.51

^plicab

32.52
16.51
Natural
Gas
Lsfy thii
—
—
-
Lsfy thi;
—
—
—
—
—
—
—
—

Le

—
—
Elec.
s regula
1.097
2.797
2.756
j regula
1.128
2.975
2.931
0.736
1.266
1.529
2.208
1.873



2.208
1.873
LPG
ion.
—
—
—
ion.
—
—
—
—
—
—
—
—



—
—
Steam

—
—
—

—
—
—
--
—
—
—
—



—
	
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 198.0
Region:    3
Data Type: 5-PEP
Page 43  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 -)
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

jplicab

46.455
25.28

Dplicab

52.9
37.815
Natural
Gas

.e

—
—

.e

—

Elec.



5.26
5.17



6.735
6.865
LPG



—
—



—

Steam



—
--



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                    FORM 5
            PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1985
Region:   3
Data Type:  5-PEP
Page 44  of 189
                            ALL UNITS ARE  IN  103  Btu/bbl.  Crude  Charged

Regulatory
Scenario
5




6



7




8




Control
Strategy
Mix
l -s
2 )
3 J
4
5
1}
3 J
4
5
1
2
3
4
5
1 -N
2 )
3 J
4
5
PURCHASED FUELS
Coal

Does

—
—
Does

—
—
	
—
—
—
—

Not. a

—
—
Oil

lot sat

27.34
15.88
lot sat

36.84
19.23
6.25
14.86
22.0
32.52
16.51

iplicab

32.52
16.51
Natural
Gas

Lsfy thl;

—
—
Lsfy thi:

—
—
	
—
—
—
—

Le

—
-
Elec.

; regulal

2.871
2.780
; regula

3.154
2.895
0.736
1.266
1.529
2.208
1.873



2.208
1.873
LPG

ion.

—
—
ion.

—
—
—
—
—
—
—



—
—
Steam



—
—


—
—
—
—
— .
—
—



—
—
SELF-GENERATED FUELS
Elec.

Refinery
Gas
—
Catalytic
Coke
—
6-

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1985
Region:  3
Data Type: 5-PEP
Page 45  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 ")
2
3 J
4
5
1 ^
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

jplicab

46.455
25.28

pplicab

52.9
37.815
Natural
Gas

Le

—
—

Le

—

Elec.



5.26
5.17



6.735
6.865
LPG



—
—



—
•
Steam



—
—

•

—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                   FORM  5

           PRIMARY ENERGY PENALTY
Industry:
Year:  1974
Region: 4
Data Type:
Page 46 of
                           ALL  UNITS ARE  IN  103  Btu/bbl.  Crude  Charged
Petroleum Refining

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 -|
2
3 J
4
5
1 ^
2
3 >
. 4
5 J
1
2
3
4
5
1 ^
2
3 J .
4
5
PURCHASED FUELS
Coal

Does

—
—


Not a


—
—
—
—
—

Not a

—
—
Oil

lot sat

4.954
2.696


pplicab


1.250
2.972
4.400
6.504
3.301

pplicab

6.504
3.301
Natural
Gas

Lsfy thi

—
—


le


—
—
—
—
—

le

—
	
Elec.

3 regula

0.355
0.308





0.147
0.253
0.306
0.442
0.375



0,442
0.375
LPG

:ion.

—
—





—
—
—
—
—



—
""
Steam



—
—





—
—
—
—
—



—

5-PEP
189
hargei
d
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-D

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year':  1974
Region:  4
Data Type: 5-PEP
Page 47 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude  Charged

Regulatory
Scenario
9




10



Control
Strategy
Mix
1 ^1
2
3 J
4
' 5
n
3 I
4
5
PURCHASED FUELS
Coal

Not a

--
—
Not i

—

Oil

pplicab

9.291
5.056
pplicab

10.58
7.563
Natural
Gas

le

—
—
le

—

Elec.



1.052
1.034


1.347
1.373
LPG



—
—


—

Steam



—
—


--

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  4
Data Type: 5-PEP
Page 48 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 1
2
3 J
4
5
1 -)
2
3 J
4
5 •
1
2
3
4
5
1 1
2
3 J
4
5
PURCHASED FUELS
Coal

Does

—
—

Does

—
—
	
—
—
—
—

Not £

—
—
Oil

not sat

34.57
19.79

not sat

25.95
15.57
6.25
14.86
22.0
32.52
16.51

pplicab

32.52
16.51
Natural
Gas

isfy thi

—
—

isfy thi

—
—
—
—
—
—
—

le

--
—
Elec.

3 regula

3.909
3.847

3 regula

2.952
2.909
0.736
1.266
1.529
2.208
1.873



2.208
1.873
LPG

;ion .

—
—

:ion .

—
—
—
—
—
—
—



—
—
Steam



—
— ,



—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region: 4
Data Type: 5-PEP
Page 49 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
•1 >
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

--

Oil

jplicab

46.455
25.28

pplicab

52.9
37.815
Natural
Gas

le

—
—

Le

—

Elec.



5.26
5.17



6.735
6.865
LPG



-.-
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
: —
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1935
Region:   4
Data Type: 5-PEP
Page 50 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
5




6


7




8




Control
Strategy
Mix
1 1
2 -
3 J
4
5
n
3 J
4
5
1
2
3
4
5
1 ^
2
3 J
4
5
PURCHASED FUELS
Coal

Does

—
—
Does
—
—
	
—
—
--
—

Not a

—
—
Oil

lot sat

39.15
24.22
lot sat
45.22
24.87
6.25
14.86
22.0
32.52
16.51

pplicab

32.52
16.51
Natural
Gas

isfy thi

—
—
isfy thi
—
—
—
—
—
—
—

le

—
—
Elec.

> regula

3.942
3.879
5 regula
5.103
5.018
- 0.736
1.266
1.529
2.208
1.873



2.208
1.873
LPG

:ion.

—
—
:ion .
—
—
—
—
—
—
—



--
—
Steam



—
—

—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                    FORM 5

            PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region: 4
Data Type: 5-PEP
Page 51 of 189
                            ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 •)
2
3 J
4
5
1 •)
2
3 •>
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not i

--

Oil

pplicah

46.455
25.28

pplicah

52.9
37.815
Natural
Gas

le

—
—

le-

—

Elec.



5.26
5.17



6.735
6.865
LPG



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-4

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1974 '
Region:   5
Data Type:  5-PEP
Page 52  of
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1
2
3
4
5
1 •)
2
3 >
4
5 J
1
2
3
4
5
1 1
2
3 J
4
5
PURCHASED FUELS
Coal
	
—
—
—
—


Not a


	
—
—
—
—

Not a

—
—
Oil
1.565
3.872
3.844
6.504
4.044


iplicab


1.25
3.704
3.674
6.504
4.044

jplicab

6.504
4.044
Natural
Gas
	
—
—
—
—


.e


—
—
—
—
—

Le

—
—
Elec.
0.156
0.298
0.272
0.442
0.395





0.138
0.289
0.261
0.442
0.395



0.442
0.395
LPG
—
—
—
—
—





—
—
—
—
--



—
—
Steam
—
—
—
—
—





—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
.Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:   5
Data Type: 5-PEP
Page 5^ of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 >
2
3 J
4
5
1 -)
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not. a

—

Oil

oplicab

9.291
6.244

pplicab

10.58
8.236
Natural
Gas

Le

—
—

Le

—

Elec.



1.052
1.076



1.347
1.391
LPG



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—


-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  5
Data Type: 5-PEP
Page 54 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5



6


•
7




8




Control
Strategy
Mix
.0
3
4
5
0
3 J
4
5
1
2
3
4
5
1 -i .
2
3 J
4
5
PURCHASED FUELS
Coal
Does
—
—
—
Does
—
—
—
	
—
—
—
—

Not a

—
—
Oil
not sat
17.4
27.6
17.82
not sat
20.07
33.20
20.81
6.25
18.52
18.37
32.52
20.22

pplicab

32.52
20.22
Natural
Gas
isfy thi
—
—
—
Isfy thi
—
—
—
—
--
—
—
—

le

—
—
Elec.
3 regula
1.407
2.058
1.898
3 regula
1.553
2.391
2.183
0.689
1.443
1.305
2.208
1.975



2.208
1.975
LPG
:ion .
—
—
—
:ion.
—
—
—
—
—
—
—
—



—
—
Steam

—
—
—

—
—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1980
Region:  5
Data Type: 5-PEP
Page 55 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 ^1
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

--

Oil

•>plicab

46.455
31.22

jplicab

52.90
41.18
Natural
Gas

.e

—
—

_e

—

Elec.



5.26
5.38



6.735
6.955
LPG



—
--



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1985
Region:  5
Data Type: 5-PEP
Page 56 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5



6




7




8




Control
Strategy
Mix
I)
3
4
5
l >
2 J
3
4 •
5
1
2
3
4
5
1 1
2 [
3 J
4
5
PURCHASED FUELS
Coal
Does
—
—
—

Does
—
—
—
—
—
—
—
—

Not a

--
—
Oil
lot sat
17.56
28.41
18.21

lot sat
18.37
32.52
20.22
6.25
18.52
18.37
32.52
20.22

jplicab

32.52
20.22
Natural
Gas
isfy chi
—
—
--

Lsfy thi
—
—
—
—
—
—
—
—

Le


—
Elec.
; regula
1.390
2.083
1.910

3 regula
1.305
2.208
1.975
0.689
1.443
1.305
2.208
1.975



2.208
1.975
LPG
:ion.
—
—
—

:ion .
—
—
—
—
—
—
—
—



—
—
Steam

—

—


—
—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                   FORM  5

           PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:   5
Data Type:  5-PEP
Page 57  of l89
                           ALL  UNITS  ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 \
2 J
3
4
5
1 1
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

>plicab

46.455
31.22

jplicab

52.90
41.18
Natural
Gas

ie

—
--

Le

—

Elec.



5.26
5.38



6.735
6.955
LPG



—
—



—

Steanj



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
.

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1974
Region:  5
Data Type: 5-PEP
Page 58 of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8
.



Control
Strategy
Mix
1
2
3
4
5
! -)
2
3 ^
4
5 J
1
2
3
4
5
1 "")
2 J
3
4
5
PURCHASED FUEL'S
Coal
—
—
—
—
—


Not a


	
—
--
--
—

Not a

—
—
Oil
1.250
2.391
4.978
6.504
2.711


pplicab


1.25
2.39
4.978
6.504
2.711

pplicab

6.504
2.711
Natural
Gas
—
—
—

—


le


—
—
—
—
—

le

—

Elec.
0.155
0.225
0.341
0.442
0.358





0.155
0.225
0.341
0.442
0.358



0.442
0.358
LPG
—
—
—
—
—





—
—
—
—
—



—
~~ ~~
Steam
—
—
—
—
—





—
'
—
—
—



—
"
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:   6
Data Type: 5-PEP
Page 59 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
l)
2 }
3
4
5
1 "1
2
3 )
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not s

—

Oil

pplicab

9.291
5.424

pplicab

10.58
7.028
Natural
Gas

le

—
—

le

—

Elec.



1.052
1.060



1.347
1.359
LPG



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1980
Region:   6
Data Type:  5-PEP
Page 60  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1
2 .
3
4
5
1
2
3
4
5
1
2
3
4
5
1 ^)
2
3 J
4
5
PURCHASED FUELS
Coal

—
—
—
—
	
—
—
•
—
	
—
—
—
—

Not a

—
—
Oil
6.250
11.96
24.89
32.52
13.56
6.250
11.96
24.89
32.52
13.56
6.25
11.955
24.89
32.52
13.555

pplicab

32.52
13.555
Natural
Gas
	
—
—
—
---
—
—
—
—
—
—
—
—
—
—

Le

—
—
Elec.
0.775
1.125
1.706
2.208
1.792
0.775 .
1.125
1.706
2.208
1.792
0.775
1.125
1.706
2,208
1.792



2.208
1.792,
LPG
—
--
—
—
—
—
—
—
—
—
—
—
—
—
—



—
—
Steam
—
—
—
—
—
--
—

—
— —
—
—
—
—
—



--
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  6
Data Type: 5-PEP
Page 61 of
                                                       189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10



Control
Strategy
Mix
1 ^
2
3 -J
4
5
n
3 ->
4
5
PURCHASED FUEL'S
Coal

Not a

—
—
Not a

—

Oil

jplicab

46.455
27.12
pplicab

52.90
35.14
Natural
Gas

Le

—
—
le

—

Elec.



5.26
5.30


6.735
6.795
LPG



—
—


—

Steam



—
—


—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:   6
Data Type: 5-PEP
Page 62 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
1 ^
2
3 J
4
5
PURCHASED FUELS
Coal
__
—
—
—
—
	
—
—
—
—
	
--
—
—
—

Not i

—
—
Oil
.6.250
11.96
24.89
32.52
13.56
6.250
11.96
24.89
32.52
13.56
6.25
11.955
24.89
32.52
13.555

pplicat

32.52
13.55f
Natural
Gas
	
—
—
—
—
—
—
—
—
—
—
—
—
—
—

le

—
—
Elec.
0.775
1.125
1.706
2.208
1.792
0.775
1.125
1.706
2.208
1.792
0.775
1.125
1.706
2.208
1.792



2.208
1.792
LPG
—
—

—
—
—
—
—
—
—
—

—
—
— —



—
—
Steam
—
—
—
—
—
—
—
—
—
—
—
—

—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                    FORM 5

            PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1935
Region:   6
Data Type: 5-PEP
Page 63 of 189
                            ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 1
2 I
3 J
4
5
1 ^
2 )
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

Dplicab

46.455
27.12

pplicab

52.90
35.14
Natural
Gas

Le

—
—

le

—

Elec.



5.26
5.30



6.735
6.795
LPG



—
—





Steam



—
—



--

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Goke
—
00

-------
                    FORM 5

            PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1974
Region:  7
Data Type: 5-PEP
Page 64 of 189
                            ALL UNITS ARE IN 103 Btu/bbl. Crude  Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 1
2
3 J
4
5
1 •)
2
3 >
4
5 J
1
2
3
4
5
1 1
2
3 J
4
5
PURCHASED FUELS
Coal

Does

--
—


Not a


	
—
—
—
—

Not a

—
—
Oil

iot sat

6.504
4.044


Dplicab


1.25
3.041
4.334
6.504
3.369

pplicab

6.504
3.369
Matural
Gas

Lsfy thi

—
—


le


—
—
—
—
—

Le

—
—
Elec.

> regula

0.442
0.395





0.146
0.256
0.302
0.442
0.376



0.442
0.376
LPG

ion .

—
—





—
—
—
—
—



—
—
Steam



—
—





—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
OQ

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:   7
Data Type: 5-PEP
Page 65 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
l"\
2 )
3
4
5
1 ^1
2
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

splicab

9.291
5.825

jplicab

10.58
7.622
Natural
Gas

le

—
—

le

—

Elec.



1.052
1.066



1.347
1.374
LPG



—
—-



--

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                    FORM 5

            PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  i960
Region: 7
Data Type- 5-PEP
Page 66 of 189
                            ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8



Control
Strategy
Mix
i v
2 }
3
4
5
1 ^1
2
3 J
4
5
1
2
3
4
5
n
3 J
4
5
PURCHASED FUELS
Coal

Does

—
—

Does

—
—
	
--

—
—
Not i

—
—
Oil

not sat

30.24
16.09

not sat

32.88
17.16
6.25
15.205
21.67
32.52
16.84!
pplicab

32.52
16.84!
Natural
Gas

isfy thi

—
—

Lsfy thi

—
--
—
—
—
—
--
le

—
—
Elec.

3 regula

2.137
1.849

3 regula

2.287
1.967
0.732
1.278
1.508
2.208
1.878


2.208
1.878
LPG

:ion.

—
—

:ion.

—
—
—
—
—
—
—


—
—
Steam



--
— —



—
—
—
—
—
—
—


~-
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke

-0

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  7
Data Type: 5-PEP
Page 67 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10



Control
Strategy
Mix
1 -)
2
3 J
4
5
n
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—
Not a

—

Oil

:>plicab

46.455
29.125
pplicab

52.90
38.11
Natural
Gas

le

—
—
le

—

Elec.



5.26
5.33


6.735
6.87
LPG



—
—


—

Steam



—
—


—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:   7
Data Type:  5-PEP
Page 68  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6



7




8




Control
Strategy
Mix
1 ^
2
3 >>
4
5
n
3 J
4
5
1
2
3
4
5
! ,
2 i
3 J •
4
5
PURCHASED FUELS
Coal

Does i

—
—
Does

—
—
	
—
—
—
—

Not a

—
—
Oil

lot sat:

30.32
16.14
tot sat:

30.80
16.41
6.25
15.205
21.67
32.52
16.845

>plicab

32.52
16.845
Natural
Gas

sfy this

—
—
.sfy thi£

—
—
_^
—
—
—
—

e

—
—
Elec.

regulat

2.146
1.858
regulat

2.200
1.914
0.732
1.278
1.508
2.208
1.878



2.208
1.878'
LPG

ion .

—
—
ion .

—
—
—
—
—
—
--



—
—
Steam



—
—


—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  7
Data Type: 5-PEP
Page 69 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 -|
2 }
3 J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a

—

Oil

pplicab

46.455
29.125

pplicab

52.90
38.11
Natural
Gas

Le

—
—

le

—

Elec.



5.26
5.33



6.735
6.87
LPG



—
—



—

Steam



—
—



—

SELF-GENERATliD FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  8
Data Type: 5-PEP
Page 70 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8



Control
Strategy
Mix
1
2
3
4
5
1 ")
2
3 \
4
5 J
1
2
3
4
5
n
3 J
4 '
5
PURCHASED FUELS
Coal
__
—
--
—
—


Not f.


	
—
—
—
—
Not i

--
—
Oil
1.250
3.374
4.004
6.504
3.709


pplicat


1.25
3.374
4.004
6.504
3.709
pplicat

6.504
3.709
Natural
Gas
	
—
—
—
—


le


—
--
—
—
—
le

—
—
Elec.
0.142
0.273
0.281
0.442
0.386





0.142'
0.273
0.28.1
0.442
0.386


0.442
0.386
LPG
	
—
—
—
—





—
—
—
—
—


—
—
Steam
—
—
—
—
—





—
—
—
—
—


—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
--

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1974
Region:  8
Data Type: 5-PEP
Page  71  of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9



10




Control
Strategy
Mix
n
3 J
4
5
1 -)
2
3 )
4
5
PURCHASED FUELS
Coal
• Not a

--
—

Not a

—

Oil
>plicab

9.291
6.037

Dplicab

10.58
7.933
Natural
Gas
Le

—
—

Le

—

Elec.


1.052
1.072



1.347
1.384
LPC


—
—



—

Steam


—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:
Year: 1980
Region:  8
Data Type:
Page 72  of
Petroleum Refining


5-PEP
189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3 .
4
5
1 -i
2' i
3 )
4
5
PURCHASED FUEL'S
Coal
__
—
—
—
—
	
—
—
—
—
	
—
--
—
—

Not 3

—
• —
Oil
6.250
16.87
20.02
32.52
18.55
6.250
16.87
20.02
32.52
18.55
6.25
16.87
20.02
32.52
18.545

pplicab

32.52
18.545
Natural
Gas
	
—
—
—
—
—
—
—
—
—
—
—
—
—
—

le

—
—
Elec.
0.710
1.363
1.406
2.208
1.930
0.710
1.363
1.406
2.208
1.930
0.71
1.363
1.406
2.208
1.930



2.208
1.930
LPG
	
—
—
—
—
—
—
—
--
—
—
—
—
—
--



—
—
Steam
	

—
—
—
—
—
—
--
—
—
—
—
—
—



—
--
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Goke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1980
Region:   8
Data Type:  5-PEP
Page 73  of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10



Control
Strategy
Mix
1 1
2
3 J
4
5
! A
3~J
4
5
PURCHASED FUELS
Coal

Not a

—
—

Not a
--

Oil

iplicab

46.455
30.185

jplicab
52.90
39.665
Natural
Gas

_e

—
—

.e
—

Elec.



5.26
5.36


6.735
6.92
LPG



—
—
•

—

Steam



—
—


--

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  8
Data Type: 5-PEP
Page 74 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8



Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
n
3 J
4
5
PURCHASED FUELS
Coal
	
--
—
—
—
	
—
—
—
—
. 	
—
—
—
—
Not a

—
—
Oil
6.250
16.87
20.02
32.52
18.55
6.250
16.87
20.02
32.52
18.55
6.25
16.87
20.02
32.52
18.545
pplicab

32.52
18.545
Natural
Gas
	
—
—
—
—
—
—
—
—
--
	
—
—
--
—
le

--
—
Elec.
0.710
1.363
1.406
2.208
1.930
0.710
1.363
1.406
2.208
1.930
0.71
1.363
1.406
2.208
1.930


2.208
1.930
LPG
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—


—
—
Steam
—
—
—
—
—
--
—
—
—
—
—
—
—
—
—


—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1935
Region:   8
Data Type: 5-PEP
Page 75 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 ^
2
3 J
4
5
1 •)
2
3 J
4
5
PURCHASED FUELS
Coal

Not £

—
—

Not c

—

Oil

pplicah

46.455
30.185

pplicat

52.90
39.665
Natural
Gas

le

—
—

le

—

Elec.



5.26
5.36



6.735
6.92
LPG



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region: 9
Data Type: 5-PEP
Page 76 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 >
2 )
3 J
4
5
1 ^
. 2
3 I
4
5 J
1
2
3
4
5
1 >>
2 1
3 J
4
5
PURCHASED FUELS
Coal

Does no

—
—


Not App.


—
—
—
—
—

Not App.

—
—
Oil

: satisi

7.318
5.176


.icable


1.25
4.162
3.218
6.504
4.509

icable

6.504
4.509
Natural
Gas

y this i

—
—





—
—
—
—
—



—
—
Elec.

egulatic

0.703
0.703





0.132
0.311
0.233
0.442
0.408



0.442
0.408
LPG

n .

— '
—





—
—
—
—
—



—
—
Steam



—
—





—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-G

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:   9
Data Type:  5-PEP
Page 77  of  189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9



10




Control
Strategy
Mix
n
3 )
4
5
1 ^
2 }
3 J
4
5
PURCHASED FUEL'S
Coal
Nof App.

—
—

Not App:

—

Oil
icable

9.291
6.530

icable

10.58
8.659
Natural
Gas


—
—



—

Elec.


1.052
1.081



1.34
1.403
LPG


—
—



—

Steam


—
—



—
s
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
o
0

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region: 9
Data Type: 5-PEP
Page 78 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 ^
2 )
3 J
4
5
1 -|
2 1
3 J
4
5
1
2
3
4
5
1 •>>
2
3 J
4
5
PURCHASED FUEL'S
Coal

Does not

—
—

Does not

—
—
	
—
—
—
—

Not App^

—
—
Oil

satisf

40.562
33.057

satisf

40.268
26.163
6.25
20.81
16.09
32.52
22.545

.icable

32.52
22.545
Natural
Gas

y this r

—
—

y this r

—
—
—
—
—
—
—



—
—
Elec.

egulatio

4.230
4.290

egulatio

3.905
3.911
0.658
1.554
1.164
2.208
2.040



2.208
2.040
LPG

i .

—
—

i.

—
—
—
—
—
—
—



—
—
Steam



—
—



—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum  Refining
.Year:  i960
Region:  9
Data Type: 5-PEP
Page  79 of  189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 ^1
2
3 J
4
5
1 >,
2 I
3 J
4
5
PURCHASED FUEL'S
Coal

Not App

—
—

Not App

—

Oil

.icable

46.455
32.65

Licable

52.90
43.295
Natural
Gas



—
—



—

Elec.



5.26
5.405



6.735
7.015
LPG



—
~ —



—

Steam



—
	



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
o

-------
                         FORM  5

                 PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  1935
Region:  9
Data Type: 5-PEP
Page 80 of 189
                                 ALL  UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
5




6




7




8




Control
Strategy
Mix
1 ")
2
3 J
4
5
1 >|
2 I
3 J
4
5
1
2
3
4
5
1 "I
2
3 J
4
5
PURCHASED FUEL'S
Coal

Does no

—
—

Does no

—
—
	
—
—
—
—

Not App

—
—
Oil

: satis:

40.877
28.743

: Satis.

42.233
29.588
6.25
20.81
16.09
32.52
22.545

.icable

32.52
22.545
Natural
Gas

y this i

—
—

y this i

—
—
—
—
—
—
—



—
—
Elec.

egulatic

4.249
4.306

egulatic

4.335
4.385
0.658
1.554
1.164
2.208
2.040



2.208
2.040
LPG

n.

—
—

n .

—
—
—
—
—
—
—



—
—
Steam



—
—



—
—
—
—
—
—
—



—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
0
(w

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1935
Region:  9
Data Type:  5-PEP
Page 81 of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
9




10




Control
Strategy
Mix
1 ^
2
3 J
4
5
1 -|
2
3 J
4
5
PURCHASED FUEL'S
Coal

Not App;

—
—

Not App;

• —

Oil

icable

46.455
32.65

icable

52.90
43.295
Natural
Gas



—
—



—

Elec.



5.26 .
5.405



6.735
7.015
LPG '



—
—



—

Steam



—
—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  1
Data Type:  5-PEP
Page 82 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14


Control
Strategy
Mix
1
2
1
2
1
2
1 .
2

PURCHASED FUEL'S
Coal

—
	
—
—
—
	
—
There w<
Oil








:re no i
Natural
Gas

—
—
—
—
—
	
—
ef inerit
Elec.

—
—
—
—
—
	
—
s in Re£
LPG

—
—
—
—
—
—
—
ion 1 in
Steam

—
—
—
—
—
—
—
1974.
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
'

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:   1
Data Type:  5-PEP
Page 83 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
	
—
—
—
	
—
	

Oil
	
—
0.08
0.125
0.08
0.125
0.08
0.125
Natural
Gas
	
-'-
—
—
—
—
—

Elec.
	
—
—
—
—
—
—

LPG
	
—
—
—
—
—
—

Steam
	
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
o

-------
                          FORM 5
                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  1935
Region:  i
Data Type: 5-PEP
Page 84 of 189
                                  ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
. 1
2
1
2
PURCHASED FUEL'S
Coal
—
— .
	
--
	
—
—

Oil
—
—
0.08
0.125
0.08
0.125
0.08
0.125
Natural
Gas
—
—
—
—
—
—
—

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
Q
-J

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  2
Data Type:  5-PEP
Page 85 of  189
                                 ALL UNITS ARE  IN  103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

' 12
13
14
Control
Strategy
Mix
1
2
1}
0

PURCHASED FUEL'S
Coal
—
—
Not A{
Not AI
Not AI
Oil
0.04
0.06
plicab!
plicab!
plicab!
Natural
Gas
—
—
e
e
e
Elec.
—
—



LPG
—
—



Steam
—
—


'
SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

o

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  2
Data Type:  5-PEP
Page 86 of  139
                                 ALL UNITS ARE  IN  103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
__
	
	
	
	
	
	

Oil
0.04
0.06
0.04
0.06
0.04
0.06
0.08
0.125
Natural
Gas
—
—
—
—
	 •
—
	

Elec.
—
—
—
—
—
—
	

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
o

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  2
Data Type: 5-PEP
Page 87 of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1'
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
—
	
—
	
—
—

Oil
0.04
0.06
0.05
0.07
0.05
0.07
0.08
0.125
Natural
Gas
—
—
—
— .
—
—
—

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  3
Data Type:  5-PEP
Page 88 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13

14
Control
Strategy
Mix
1
2
1 1
2 J
l)
2 j

PURCHASED FUEL'S
Coal
—
' —
Not A]

Not A]

Not AI
Oil
0
0
plicab;

plicab;

plicab;
Natural
Gas
—
—
e

e

e
Elec.
—
—





LPG
—
—





Steam
—
—





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  3
Data Type:  5-PEP
Page 89 of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
—
—
—
	
—
	

Oil
0
0
0.03
0.05
0.03
0.05
0.08
0.125
Natural
Gas
—
—
—
—
—
—
—

Elec.
—
—
—
—
—
—
—
i
LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
.Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:   3
Data Type: 5-PEP
Page 90 of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude  Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
	

	
—
	
—
	

Oil
0
0
0.04
0.06
0.04
0.06
0.08
0.125
Natural
Gas
—
—
	
—
—
—
—

Elec.
• —
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

S t earn
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  '1974
Region:  4
Data Type: 5-PEP
Page 91 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1 "I
2 J
O
2 J
o
2 J
PURCHASED FUEL'S
Coal
—
—
Not AI

Not AI

Not AI

Oil
0.05
0.08
plicab!

plicab!

plicabi

Natural
Gas
—
—
e

e

e

Elec.
—
—






LPG
—
—





V
Steam
—
—






SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  4
Data Type:  5-PEP
Page 92 of  189
                ALL UNITS ARE IN 103 Btq/bbl. Crude Charged

Regulatory
Scenario
11

12

13

. 14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
—
	
—
—
—
—

Oil
0.05
0.08
0.05
0.08
0.05
0.08
0.08
0.125
Natural
Gas
—
—
—
—
—
—
—~

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:     A
Data Type: 5-PEP
Page 93  of l89
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
'• —
	
—
—
—
	

Oil
0.05
0.08
0.05
0.08
0.05
0.08
0.08
0.125
Natural
Gas
—
—
—
—
—
—
—

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec .
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:    5
Data Type: 5-PEP
Page 94  of  189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13
14

Control
Strategy
Mix
1
2
n
2)
0
M
2 j
PURCHASED FUEL'S
Coal
—
—
Not. A

Not A
Not A

Oil
0.02
0.03
iplicab;

>pl±cab.
iplicab!

Natural
Gas
—
—
e

e
e

Elec.
—
—





LPG
—
—





Steam
—
—





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
-

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  5
Data Type: 5-PEP
Page 95 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
•1
2
PURCHASED FUELS
Coal
—
—
—
—
	
—
—

Oil
0.02
0.03
0.03
0.04
0.03
0.04
0.08
0.125
Natural
Gas
—
—
—
—
—
—
—

Elec.
—
—
. —
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  5
Data Type:  5-PEP
Page 96 of 189
                ALL UNITS ARE IN.103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1..
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
::
—
	
—
	
—
—

Oil
0.02
0.03
0.03
0.05
0.03
0.05
0.08
0.125
Natural
Gas
__
—
	
—
	
—
—

Elec.
__
—
	
—
—
—
—

LPG
__
—
	
. —
—
—
—

Steam
__
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                          FORM  5
                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  6
Data Type: 5-PEP
Page 97 of 189
                                  ALL UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
11

12
13
14

Control
Strategy
Mix
!\
2J
2J
1 i
!\
2
PURCHASED FUELS
Coal
	 	
—
Not Af
Not Ap
Not A{

Oil
0.01
0.02
plicabl
plicabl
plicabl

Natural
Gas
	
—
e
e
e

Elec.
	
	




LPG
	
—




Steam
	
—




SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

Po

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  6
Data Type:  5-PEP
Page 98 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
; —
—
—
—
—
—

Oil
0.01
0.02
0.01
0.02
0.01
0.02
0.08
0.12
Natural
Gas
—
—
—
—
—
—
—

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:'  6
Data Type: 5-PEP
Page 99 of  189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
' 1
2
1
2
PURCHASED FUEL'S
Coal
—
—
—
—
—
—
—

Oil
0.01
0.02
0.01
0.02
0.01
0.02
0.08
0.12
Natural
Gas
—
—
—
—
—
—
—

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
— .
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:   7
Data Type: 5-PEP
Page 100 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12
13
'14
Control
Strategy
Mix
1
2
0
I]

PURCHASED FUEL'S
Coal
—
—
Not A
Not A
Not A
Oil
0
0
iplicab!
>plicat>;
iplicalx
Natural
Gas
—
—
e
.e
e
Elec.
—
—



LPG
—
—



Steam
—
—



. SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  7
Data Type: 5-PEP
Page 101 of 189
                                 ALL UNITS ARE  IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUELS
Coal
—
—
—
—
	
—
	

Oil
0
0
0
0
0.01
0.01
0.08
0.12
Natural
Gas
—
—
—
—
—
—
—

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
R;

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   1935
Region:   7
Data Type: 5-PEP
Page 102 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
' 2
PURCHASED FUEL'S
Coal
—
—
	
—
	
—
—

Oil
0
0
0
0
0.01
0.02
0.08
0.12
Natural
Gas
—
—
	
—
—
—
—

Elec.
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   1974
Region:  8
Data Type:  5-PEP
Page 103 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14
Control
Strategy
Mix
1
2
1 1
2 J
1 "1
2 j
1 1
PURCHASED FUEL'S
Coal
—
—
Not A{

Not A[

Not AI
Oil
0
0
plicab]

plicab!

plicab;
Natural
Gas
—
—
e

e

e
Elec.
—
—





LPG
—
—





Steam
—
—





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  8
Data Type: 5-PEP
Page 104 of 189
                ALL UNITS ARE IN  103  Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUELS
Coal
—
—
—
—
	
—
—

Oil
0
0
0
0
0
0
0.08
0.12
Natural
Gas
—
—
—
—
—
—
—

Elec..
—
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
-•-
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:    1985
Region:   8
Data Type: 5-PEP
PagelOS of  189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
—
	
—
	
— .
	

Oil
0
0
0
0
0
0
0.08
0.12
Natural
Gas
—
—
	
—
—
—
	

Elec.
—
—
	
—
—
—
	

LPG
—
—
	
—
—
—
—

Steam
—
— -
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
00

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   1974
Region:   9
Data Type: 5-PEP
Page 106 of  189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12


13
14
Control
Strategy
Mix
1
2
i"!
2 ?
*- J
\]

PURCHASED FUEL'S
Coal
—
• —
Not Af


Not Aj
Not Ay
Oil
0
0
plicabl


plicabl
plicabl
Natural
Gas
—
—
e


e
e
Elec.
—
—





LPG
—
—





Steam
—
—





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  9
Data Type:  5-PEP
Page 107 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
' 2
1
2
PURCHASED FUEL'S
Coal
	
—
—
—
—
—
	

Oil
0
0
0
0
0.02
0.02
0.08
0.12
Natural
Gas
	
—
—
—
—
—
—

Elec.
	
—
—
—
—
—
—

LPG
—
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
Q

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  9
Data Type: 5-PEP
Page 108 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
11

12

13

14

Control
Strategy
Mix
1
2
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
	
—
	
—
—
—
—

Oil
0
0
0
0
Q.01
0.02
0.08
0.12
Natural
Gas
	
—
	
—
—
— •
—

Elec.
	
—
—
—
—
—
—

LPG
	
—
—
—
—
—
—

Steam
—
—
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    1
Data Type: 5-PEP
Page 109 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUELS
Coal
There we












Oil
re no r












Natural
Gas
ef inerie












Elec.
3 in Reg












LPG
.on I in












Steam
1974.












SELF-GENERATED FUELS
Elec.

Refinery
Gas
•
Catalytic
Coke

Go

-------
                         FORM  5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:     l
Data Type: 5-PEP
Page 110 of 189
                                 ALL  UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1 1
2}
3
4
1 )
2\
3
• 4
1 )
2}
3
4
1
PURCHASED FUEL'S
Coal

Does nc
—
Far exc

Does nc
—
Far exc

Does nc
—
Far exc

Oil

t satis
0.336
eeds tt

t satis
0.336
eeds tt

t satis
0.336
eeds tl
0.336
Natural
Gas

fy this
—
e requir

fy this
—
e requir

fy this
—
e requir

Elec.

regulati
0.024
ements o

regulati
0.024
ements o

regulati
0.024
ements o
0.024
LPG

an
—
E this r

Dn
—
f this r

3n
—
f this r

Steam


—
igulati


' —
igulati-


—
;gulati<





>n



m



m

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
U)

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:     i
Data Type: 5-PEP
Page 111. of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude  Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
n
2 f D°
J
4 Fa
n.
2JDo
3
4 Fa
n
,2JDo
3
4 Fa
1
PURCHASED FUEL'S
Coal

is not mi
—
" exceed:

js not m<
—
' exceed:

:s not mi
—
: exceed:

Oil

et thi:
0.336
the re

:et this
0.336
the rt

et thi:
0.336
i the rt
0.336
Natural
Gas

regulat
—
quiremer

regulat
—
quiremer

regulat
—
quiremer

Elec.

ion
0.0024
ts of th

ion
0.024
ts of tr

ion
0.024
ts of th
0.024
LPG


—
is regul


—
is regul


—
is regul

Steam


—
ation


—
ation


—
ation

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    2
Data Type: 5-PEP
Page 112 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
15



16


17


18
Control
Strategy
Mix
n
2 ) D°
_/
4 Fa
il
2 I
3 No
4
J
\~\
3 S No
4
1 No
PURCHASED FUEL'S
Coal

;s not s;
—
• exceed:


: Applic;

: Applic;

: Applic;
Oil

tisfy I
0.336
the r£


ble

ble

ble
Natural
Gas

his regt
—
quiremer







Elec.

lation
0.024
ts of tli







LPG


—
is regul







Steam


—
it ion







SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    2
Data type: 5-PEP
Page 113 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
I"!
2J D°<
3
4 Fa
1\
2 j D°<
3
4 Fai
n
2 j *»
3
4 Fai
1
PURCHASED FUELS
Coal

s not S£
—
exceeds

s not Si
—
exceeds

s not si
—
exceeds

Oil

tisfy t
0.336
the re

tisfy t
0.336
the re

tisfy t
0.336
the re
0.336
Natural
Gas

his regu
—
quiremen

his regu
—
quiremen

his regu
—
quiremen

Elec.

lation
0.024
ts of th

lation
0.024
ts of th

lation
0.024
ts of th
0.024
LPG


—
Ls regul


—
Ls regul


—
Ls regul

Steam


—
ition


—
ition


—
ition

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
•
Go

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    2
Data Type: 5-PEP
Page 114 of 189
                                 ALL UNITS ARE IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
n
2JDoe
3
4 Far
n
2JDoe
3
4 Far
n
2JDoe
3J
4 Far
1
PURCHASED FUEL'S
Coal

» not sa
—
exceeds

3 not sa
—
exceeds

3 not sa
—
exceeds

Oil

-isfy tl
0.336
the re<

:isfy tl
0.336
the re<

:isfy tl
0.336
the re<
0.336
Natural
Gas

iis regu]
—
uirement

iis regu]
—
[iiirement

iis regu]
—
[uiremenl

Elec.

ation
0.024
s of thi

ation
0.024
s of thi

ation
0.024
s of thi
0.024
LPG


—
s regula


—
s regula


—
s regula

Steam


—
tion


—
tion


—
tion

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
Ovi

-------
                         FORM  5

                PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    3
Data Type: 5-PEP
Page 115 of 189
                                 ALL UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15

16


17



18
Control
Strategy
Mix
1
0
A
2 1
•'}
1
2~]
3 I
4
1
PURCHASED FUEL'S
Coal
—
Far exc


Not App


Not App

Not App
Oil
0.336
ieds th


Licable


Licable

Licable
Natural
Gas
—
: requir<








Elec.
—
:ments ol








LPG
—
this re








Steam
—
gulatic








SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

Go
00

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:     3
Data Type: 5-PEP
Page 116 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
15



16


17



18
Control
Strategy
Mix
1
2 1
3
4 J
1
2 1
«'
~s
21
3
4 I
1
PURCHASED FUEL'S
Coal
	

Far exct

	

Far exce
__

Far exct


Oil
0.336

eds the

0.0336

eds the
0.336

eds the

0.336
Natural
Gas
	

require

	

require
__

require


Elec.
	

ments of

	

ments of
__

ments of

0.024
LPG
	

this re

	

this re
__

this re

.
Steam
	 	

>ulatio

	

'ulatio
	

julatio


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    3
Data Type: 5-PEP
Page 117 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15

16

17


18
Control
Strategy
Mix
1
3 1
1
3 I
•'•-x
21
;]
i
PURCHASED FUELS
Coal

Far exct
—
Far exec
	

Far exce

Oil
0.336
eds the
0.336
eds the
0.336

eds the
0.336
Natural
Gas
—
require
—
require
	

require

Elec.
—
ments of
—
men t s of
__

ments of
0.024
LPG
—
this re
—
this re
__

this re

Steam
—
»ulatio
—
'ulatio


>ulatio

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    4
Data Type: 5-PEP
Page 118 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
15



16



17


18
Control
Strategy
Mix
ll
2
3 J
4
n
2
• 'J
' 4
|]
3.J
4
1
PURCHASED FUEL'S
Coal

Does nol

—


Not App!


Not App:

Not App!
Oil

satis!

0.336


.icable


.icable

.icable
Natural
Gas

y this i

—








Elec.

egulatio

0.024








LPG

n

—








Steam



—








SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    4
Data Type: 5-PEP
Page 119 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17


18
Control
Strategy
Mix
0
2
3J
J
o
2 1
3j
4
il
•5
J J
4
1
PURCHASED FUEL'S
Coal

Does noi

—

Does nol

—

Does no
—

Oil

satisi

0.336
-
satis

0.336

: satis
0.336
0.336
Natural
Gas

y this i

—

y this J

—

y this i
—

Elec.

egulatio

0.024

egulatio

0.024

egulatic
0.024
0.024
LPG

n

—

n

—

n
—

Steam



— •



—


—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    4
Data Type: 5-PEP
Page 120 of 189
                                 ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15




16



17



18
Control
Strategy
Mix
•v
1
2
3 1
*S
4
l]
2
3J
4
l]
2
3J
. ^/
1
PURCHASED FUEtS
Coal

Does noi


—

Does noi

—

Does no

—

Oil

: satis:


0.336

: satis

0.336

,. satis

0.336
0.336
Natural
Gas

y this i


—

y this T

—

y this i

—

Elec.

egulatic


0.024

egulatic

0.024

egulatic

0.024
0.024
LPG

n


—

n

—

n

—

Steam




—



—



—

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
U

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1974
Region:5
Data Type:  5-PEP
Page 121 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16


17


18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4






1
PURCHASED FUEL'S
Coal
Does no
Does no
—
Far exc

Not App


Not App

Not App
Oil
: satis
: satis
0.336
jeds th

.icable


.icable

. icable
Natural
Gas
:y this
:y this
—
; requiri







Elec.
•egulatit
•egulatii
0.024
:ments oi







LPG
m.
in- <*
—
this re







Steam


—
gulatic







SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region: 5
Data Type: 5-PEP
Page 122 of 189
                                 ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUEL'S
Coal
Does nol
Does not
—
Far exct
Does not
Does not
—
Far exct
Does not
Does not
—
Far exce

Oil
satisi
satisi
0.336
eds the
satisi
satisf
0.336
eds the
satisf
satisf
0.336
eds the
0.336
Natural
Gas
y this r
y this r
—
require
y this r
y this r
—
require
y this r
y this r
—
require

Elec.
egulatio
egulatio
0.024
ments of
egulatio
egulatio
0.024
uents of
egulatio
agulatio
0.024
nents of
0.024
LPG
a.
n.
—
this re
i.
i.
—
this re
i.
i.
—
this re

Steam


—
julatio


—
julatio


—
>ulatioi

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-C

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   1935
Region:  5
Data Type: 5-PEP
Page 123 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
. 3
4
1
2
3
4
1
PURCHASED FUEL'S
Coal
Does not
Does no I
—
Far exce
Does not
Does not
—
Far exce
Does not
Does not
—
Far exce

Oil
satisl
satisf
0.336
eds the
satisi
satisi
0.336
eds the
satisf
satisf
0.336
eds the
0.336
Natural
Gas
y this r
y this r
—
require
y this r
y this r
—
require
y this r
y this r
—
require

Elec.
egulatio
egulatio
0.024
ments of
egulatio
egulatio
0.024
nents of
egulatio
agulatio
0.024
nents of
0.024
LPG
i.
n.
—
this re
\.
i.
—
this re
i .
\.
—
this re

Steam


—
;ulatio


—
julatioi


—
;ulatioi

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM  5

                 PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:6
Data Type: 5-PEP
Page 124 of 189
                                 ALL  UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15



16


17


18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4






1
PURCHASED FUELS
Coal
Does no
—
Far exci
Far exci

Not App!


Not App!

Not App^
Oil
: satis:
0.336
ieds thi
:eds thi

.icable


.icable

.icable
Natural
Gas
y this i
—
: require
: require







Elec.
egulatic
0.024
ments oi
ments oi







LPG
n.
—
this re
this re







Steam

—
gulatio
gulatio







SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

-C
—J

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1980
Region:6
Data Type: 5-PEP
Page 125 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
I
PURCHASED FUEL'S
Coal
Does no
—
Far exc
Far exc
Does no
—
Far exc<
Far exc<
Does no
—
Far exec
Far exc(

Oil
_ satis
0.336
;eds th(
:eds thi
: satis
0.336
;eds th<
:eds th(
: satis;
0.336
eds th<
ieds the
0.336
Natural
Gas
y this i
—
- require
require
y this i

require
require
y this i
—
require
require

Elec.
egulatic
0.024
ments oi
rnents ol
egulatic
0.024
ments of
ments oi
egulatic
0.024
ments of
ments of
0.024
LPG
n.
—
this re
this re
n.
—
this re
this re
n.
—
this re
this re

Steam

—
gulatio
gulatio

—
gulatio
gulatio

—
gulatio
'ulatio

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   1935
Region:   6
Data Type: 5-PEP
Page 126 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUELS
Coal
Does no
—
Far exc
Far exci
Does no
—
Far exc<
Far exci
Does no
—
Far exec
Far exce

Oil
: satis
0.336
:eds thi
:eds thi
satis
0.336
;eds the
ieds the
satisJ
0.336
eds the
eds the
0.336
Natural
Gas
:y this i
—
'. require
: require
y this i
—
require
require
y this i
—
require
require

Elec.
egulatic
0.024
ments oi
ments oi
egulatic
0.024
ments of
ments oi
egulatic
0.024
ments of
ments of
0.024
LPG
n.
—
this re
this re
n.
—
this re
this re
n.
—
this re
this re

Steam

—
gulatio
gulatio

—
gulatio
gulatio

—
^ulatio
^ulatio

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1974
Region:  7
Data Type: 5-PEP
Page 127 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
15



16


17


18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
'2
3
4






1
PURCHASED FUELS
Coal
Does no
Does no
—
Far exc

Not App


Not App

Not App
Oil
t satis
t satis
0.336
3eds th

Licable


.icable

.icable
Natural
Gas
:y this
:y this
—
; requin







Elec.
egulatif
•egulatic
0.024
;ments oJ







LPG
n.
n.
—
this r£

•





Steam


—
gulatic







SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

Ol
0

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:7
Data Type: 5-PEP
Page 128 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
15



16



17



.18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUEL'S
Coal
Does no
Does no
—
Far exc
Does no
Does no
—
Far exc
Does no
Does no
—
Far exc«

Oil
: satis
: satis
0.336
:eds th(
: satis
: satis:
0.336
;eds thi
: satis
satis:
0.336
leds tht
0.336
Natural
Gas
:y this .1
:y this i
—
'. require
:y this i
y this i
—
require
y this i
y this i
—
require

Elec.
egulatic
egulatic
0.024
ments oi
egulatic
egulatic
0.024
ments oi
egulatic
egulatic
0.024
ments of
0.024
LPG
n.
n.
—
this re
n.
n.
—
this re
n.
n.
—
this re

Steam


—
gulatio


—
gulatio


—
gulatio

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
G|

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  7
Data Type: 5-PEP
Page 129 of 189
                                 ALL UNITS ARE  IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUEL'S
Coal
Does not
Does nol
—
Far exc(
Does nol
Does nol
—
Far exci
Does no
Does no
—
Far exc(

Oil
satisl
satisf
0.336
eds the
satis
satis
0.336
eds the
satisJ
satisJ
0.336
eds the
0.336
Natural
Gas
y this r
y this i
—
require
y this i
y this r
—
require
y this i
y this i
—
require

Elec.
egulatio
egulatio
0.024
ments of
egulatio
egulatio
0.024
ments of
egulatic
egulatio
0.024
ments of
0.024
LPG
n.
n.
—
this re
n.
n.
—
this re
n.
n.
—
this re

Steam


—
;ulatio


—
*ulatio


—
>ulatio

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
Oi

-------
                         FORM  5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   1974-
Region:  8
Data Type: 5-PEP
Page 130 of 189
                                 ALL  UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15



16


17


18
Control
Strategy
Mix
1
2
3
4
1 ,
2
3
. 4
1
2
3
4






1
PURCHASED FUEL'S
Coal
Does no
Does no
—
Far exc

Not App


Not App!

Not App:
Oil
: satis
: satis
0.336
:eds thi

.icable


.icable

icable
Natural
Gas
y this j
:y this i
—
: require







Elec.
egulatic
egulatic
0.024
ments of







LPG
n.
n.
—
this re







Steam


—
gulatio







SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

Ul

-------
                         FORM 5

                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:  1980
Region:  8
Data Type: 5-PEP
Page 131 of  189
                                 ALL UNITS ARE IN 103  Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUEL'S
Coal
Does no
Does no
—
Far exc
Does no
Does no
—
Far exc
Does no
Does no
—
Far exc

Oil
t satis
t satis
0.336
eeds th
t satis
t satis
0.336
jeds th
t satis
: satis
0.336
;eds th
0.336
Natural
Gas
:y this
:y this
—
e requir
:y this
fy this
—
* requir
:y this
.y this
—
i requin

Elec.
regulati
regulati
0.024
sments o
regulati
•egulati
0.024
;ments o
:egulati<
•egulati
0.024
nnents o
0.024
LPG
m.
m.
—
: this r<
m.
>n.
—
: this re
m.
>n.
—
this re

Steam


—
gulatic


—
gulatic


—
gulatic

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
Oi
-XT

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1985
Region:  8
Data Type: 5-PEP
Page 132 of 189
                                 ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUEL'S
Coal
Does not
Does not

Far exct
Does not
Does not
—
Far exce
Does not
Does not
—
Far exce

Oil
satisf
satisi
0.336
eds t\\t
satisi
satisf
0.336
eds the
satisf
satisf
0.336
eds the
0.336
Natural
Gas
y this r
y this r
—
require
y this r
y this r
—
require
y this r
y this r
—
require

Elec.
egulatio
egulatio
0.024
nents of
egulatio
egulatio
0.024
nents of
egulatio
egulatio
0.024
nents of
0.024
LPG
i.
i.
—
this re
i.
i.
—
this re
i.
i.
—
this re

Steam


—
*ulatio


—
;ulatio


—
'ulatioi

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
Cr.

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   1974
Region:  9
Data Type: 5-PEP
Page 133 of . 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17


18
Control
Strategy
Mix
1
2
3
4
I
2
3
4
1
2
3
4







1
PURCHASED FUEL'S
Coal
Does no
Does noi
—
Far exci


Not App";


Not App;

Not App!
Oil
satis
satis
0.336
eds the


.icable


icable

icable
Natural
Gas
y this i
y this i
—
require








Elec.
egulatic
egulatic
0.024
ments of








LPG
n.
n.
—
this re








Steam


—
gulatio








SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

0)

-------
                          FORM 5
                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:   1980
Region:   9
Data Type: 5-PEP
Page 134 of 189
                                  ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4'
1
2
3
4
1
PURCHASED FUEL'S
Coal
Does noi
Does no
—
Far exc<
Does nol
Does nol
—
Far exc(
Does no I
Does not
—
Far exco

Oil
satis:
: satis:
0.336
;eds the
satisi
satisi
0.336
eds the
satisf
satisf
0.336
eds the
0.336
Natural
Gas
y this i
y this r
—
require
y this i
y this r
—
require
y this r
y this i
—
require

Elec.
egulatic
egulatic
0.024
ments of
egulatic
egulatio
0.024
ments of
egulatio
egulatio
0.024
ments of
0.024
LPG
n.
n.
—
this re
n.
n.
—
this re
n.
n.
—
this re

Steam


—
gulatio


—
gulatio


—
>ulatio

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-J

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:  1935
Region: 9
Data Type: 5-PEP
Page 135 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
15



16



17



18
Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1
PURCHASED FUELS
Coal
Does no
Does no
—
Far exc
Does no
Does no
—
Far exc
Does no
Does no
—
Far exc

Oil
: satis
: satis
0.336
jeds th
: satis
: satis
0.336
:eds th
: satis
: satis
0.336
ieds th
0.336
Natural
Gas
:y this i
:y this i
—
: requin
:y this :
:y this :
—
i requir<
:y this
:y this
—
; require

Elec.
egulatic
egulatic
0.024
:ments o:
•egulatic
egulatic
0.024
ments o
egulatic
egulatic
0.024
:ments oi
0.024
LPG
n.
n.
—
this r«
n.
n.
—
this re
n.
n.
—
this re

Steam


—
gulatic


—
gulatic
0

—
gulatic

SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke


-------
                           FORM 5
                   PRIMARY ENERGY PENALTY
                                         Industry:  Petroleum Refining
                                         Year:       1974
                                         Region:     1
                                         Data  Type: 5-PEP
                                         Page 136 of 189
                                    ALL  UNITS ARE IN 103  Btu/bbl.  Crude Charged
             Regulatory
             Scenario
                19
                20
                21
Control
Strategy
  Mix
   1

   2

   1

   2

   1

   2
                                             PURCHASED  FUEL'S
Coal
Oil
Natural
  Gas
                                                   Tht
Elec.
                                                      re were
LPG
Steam
                                     no refineries ii Region
                                                                 SELF-GENERATED FUELS
Elec.
                                                   in 1974
Refinery
  Gas
Catalytic
  Coke
-0

-------
       . FORM 5
PRIMARY ENERGY PENALTY
Industry:
Year:
Region:
Data Type:
Page 137 of
Petroleum Refining
1980
1
5-PEP
189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1 >

PURCHASED FUELS
Coal
'. —
—
—
—

Not App]
Oil
9.4
6.2
16.3
10.5

icable
Natural
Gas
	
—
—
—


Elec.
0.3
0.2
0.3
0.2


LPG
	
—
—
—


Steam
	
—
—
—


SELF-GENERATED FUELS
Elec.
	
—
—

Refinery
Gas
	
—
—

Catalytic
Coke
2.8
1.9
6.9
4.6

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    1
Data Type: 5-PEP
Page 138 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
.-. —
—
—
—


Oil
44.4
29.3
44.4
29.3
45.8
30.2
Natural
Gas
—
—
—
—
—

Elec.
1.3
0.9
1.3
0.9
1.3
0.9
LPG
—
—
—
—
—

Steam
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
—
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
16.9
11.2
16.9
11.2
16.9
11.2

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    2
Data Type: 5-PEP
Page 139 of 189
                ALL UNITS ARE  IN  103  Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
s



>


PURCHASED FUEL'S
Coal
—


Not Ap


Oil
0


plicabl


Natural
Gas
—


e


Elec.
0





LPG
—





Steam
—





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0

-------
                         FORM  5

                 PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    2
Data Type: 5-PEP
Page 140 of 189
                                 ALL  UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
19

20

21
Control
Strategy
Mix
1
2
1
2

PURCHASED FUEL'S
Coal
—
—
—
—
Not App
Oil
9.4
6.2
16.3
10.5
licable
Natural
Gas
—
—
—
—

Elec.
0.3
0.2
0.3
0.2
-
LPG
—
—
—
—

Steam
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
—

Refinery
Gas
—
—
—

Catalytic
Coke
2.8
1.9
6.9
4.6
Go

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:     2
Data Type: 5-PEP
Page 141 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal

—
—
—
—

Oil
21.2
14.1
21.2
14.1
22.6
14.9
Natural
Gas
—
—
—
—
—

Elec.
0.7
0.5
0.7
0.5
0.7
0.5
LPG
—
—
—
—
—

Steam
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
—
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
9.2
6.1
9.2
6.1
9.2
6.1

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    3
Data Type: 5-PEP
Page 142 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2



'


PURCHASED FUEL'S
Coal



Not App]


Oil
0


icable


Natural
Gas
—





Elec.
0





LPG
—





Steam
—





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0

-------
        FORM 5
PRIMARY ENERGY PENALTY .
Industry:  Petroleum Refining
Year:      1980
Region:    3
Data Type: 5-PEP
Page 143 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21
Control
Strategy
Mix
1
2
1
2

PURCHASED FUELS
Coal
—
—
—
—
Not App
Oil
9.4
6.2
L6.3
10. 5
Licable
Natural
Gas
—
—
—
—

Elec.
0.3
0.2
0.3
0.2

LPG
—
—
—
—

Steam
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
—

Refinery
Gas
—
—
—

Catalytic
Coke
2.8
1.9
6.9
4.6

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:     3
Data Type: 5-PEP
Page 144 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
: 	
	
	
	
	

Oil
21.2
14.1
21.2
14.1
22.6
14.9
Natural
Gas
—
—
—
—
—

Elec.
0.7
0.5
0.7
0.5
0.7
0.5
LPC
—
—
—
—
—

Steam
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
—
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
9.2
6.1
9.2
6.1
9.2
6.1

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    4
Data Type: 5-PEP
Page 145 of 189
                                 ALL UNITS ARE  IN  103  Btu/bbl.  Crude  Charged

Regulatory
Scenario
19


20

21

Control
Strategy
Mix
1
X
2
1
2
1
2 ,




>


PURCHASED FUEL'S
Coal



Not App



Oil
0


licable



Natural
Gas







Elec.
0






LPG







Steam







SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0
CO

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:   .   1980
Region:    4
Data Type: 5-PEP
Page 146 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
I ~}

PURCHASED FUEL'S
Coal
—
—
—
—

Not App
Oil
6.9
4.6
L3.5
8.9

licable
Natural
Gas
—
—
—
—


Elec.
0.3
0.2
0.5
0.3


LPG
—
—
—
—


Steam
—
—
—
—


SELF-GENERATED FUELS
Elec.
—

Refinery
Gas
—

Catalytic
Coke
3.7
2.5

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:
Year:
Region:     4
Data Type: 5-PEP
Page 147 of 189
Petroleum Refining
1985
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
	
—
—
—
—

Oil
21.4
14.1
21.4
14.1
24.0
16.0
Natural
Gas
	
—
—
—
—

Elec.
0.5
0.3
0.5
0.3
0.7
0.5
LPG
	
—
—
—
—

Steam
	
—
—
—
• —

SELF-GENERATED FUELS
Elec.
__
—
—
—
—
-
Refinery
Gas
	
—
—
—
—

Catalytic
Coke
7.0
4.6
7.0
4.6
5.9
3.9

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    5
Data Type: 5-PEP
Page 148 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2



•


PURCHASED FUEL'S
Coal
• —


Not App


Oil
0


licable


Natural
Gas
—





Elec.
0





LPG
	





Steam
	





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    5
Data Type: 5-PEP
Page 149 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
M
2 J
PURCHASED FUEL'S
Coal
—
—
—
—
Not App

Oil
6.0
4.0
13.5
8.9
licable

Natural
Gas
—
—
—
—


Elec.
0.2
0.1
0.5
0.3


LPG
—
—
—
—


Steam
	
—
—
—


SELF-GENERATED FUELS
Elec.
	
—
—

Refinery
Gas
	
—
—

Catalytic
Coke
1.2
0.8
3.0
1.9

-------
                          FORM 5

                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1935
Region:    5
Data Type: 5-PEP
Page 150 of 189
                                  ALL UNITS ARE IN 103  Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUELS
Coal
—
—
—
—
—

Oil
20.9
13.8
20.9 •
13.8
25.3
16.7
Natural
Gas
—
—
—
—
—

Elec.
0.8
0.5
0.8
0.5
1.0
0.7
LPG
—
—
—
—
—

Steam
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
—
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
4.4
2.9
4.4
2.9
4.4 .
2.9
Go

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:     6
Data Type: 5-PEP
Page 151 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2






PURCHASED FUEL'S
Coal
—


Not App]


Oil •
0


icable


Natural
Gas
—


in 1974


Elec.
0





LPG
—





Steam
—





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    6
Data Type: 5-PEP
Page 152 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1 ->

PURCHASED FUEL'S
Coal
—
—
—
—

Not Appi
Oil
5.7
3.8
11.3
7.5

.icable
Natural
Gas
—
—
—
—


Elec.
0.3
0.2
0.5
0.3


LPG
—
—
—
—


Steam
—
—
—
—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    6
Data Type: 5-PEP
Page 153 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
—
—
—
—

Oil
33.2
21.9
33.2
21.9
37.5
24.8
Natural
Gas
—
—
—
—
—

Elec.
1.3
0.9
1.3
0.9
1.4
0.9
LPG
	
—
—
—
—

Steam
	
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
—
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
1.8
1.2
1.8
1.2
5.0
3.0

-------
                          FORM 5

                  PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    7
Data Type: 5-PEP
Page 154 of 189
                                  ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19


20

21

Control
Strategy
Mix
1
-v
2
1
2
1
2 .,




>


PURCHASED FUEL'S
Coal




Not App!


Oil -
0



icable


Natural
Gas




in 1974


Elec.
0





•
LPG
__





•
Steam
	






SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0
-J

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    7
Data Type: 5-PEP
Page 155 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1 ^
2]
PURCHASED FUEL'S
Coal
• —
—
—
—

Not App!
Oil
15.8
10. A
21.9
14.5
.
icable
Natural
Gas
	
—
--
—


Elec.
0.6
0.4
0.7
0.5


LPG
	
—
—
—


Steam
__
—
—
—


SELF-GENERATED FUELS
Elec.
_
—
—

Refinery
Gas
__
—
—

Catalytic
Coke
1.3
0.9
5.4
3.6

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    7
Data Type: 5-PEP
Page 156 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
-
—
—
—

Oil
23.5
15.5
23.5
15.5
25.8
17.0
Natural
Gas
—
—
-^
—
—

Elec.
0.8
0.6
0.8
0.6
0.8
0.6
LPG
—
—
—
—
—

Steam
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
	
—
—
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
6.0
4.0
6.0
4.0
7.0
4.6

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    8
Data Type: 5-PEP
Page 157 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
• 19

20

21

Control
Strategy
Mix
1
2 1
1
2
1
2






PURCHASED FUELS
Coal
	


Not Appl


Oil
0


icable


Natural
Gas
	


in 1974


Elec.
0





LPG
	





Steam
	





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    8
Data Type: 5-PEP
Page 158 of 189
                ALL UNITS ARE IN  103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
M
2 J
PURCHASED FUEL'S
Coal
—
—
—
—
Not App

Oil
5.7
3.8
11.3
7.5
Licable

Natural
Gas
—
—
—
—


Elec.
0.3
0.2
0.5
0.3


LPG
	
—
—
—


Steam
	
—
—
—


SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    8
Data Type: 5-PEP
Page 159 of 189
                                 ALL UNITS ARE IN  103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
—
—
—
—

Oil
33.2
21.9
33.2
21.9
37.5
24.8
Natural
Gas
—
—
—
—
—

Elec.
1.3
0.9
1.3
0.9
1.4
0.9
LPG
—
—
—
—
—

Steam
—
—
—
—
—

SELF- GENERATED FUELS
Elec.
—
—
—
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
1.8
1.2
1.8
1.2
5.0
3.0
00

-------
                         FORM  5
                 PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    9
Data Type: 5-PEP
Page 160 of  189
                                 ALL  UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
.1
2
1
2
*^



»


PURCHASED FUEL'S
Coal
—


Not App!


Oil
0


icable


Natural
Gas
—





Elec.
0





LPG
	





Steam
	





SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
0
U

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    9
Data Type.: 5-PEP
Page 161 of 189
                ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
19

20

21
Control
Strategy
Mix
1
2
1
2

PURCHASED FUELS
Coal
—
—
—
—
Not Appl
Oil
3.6
2.4
3.9
2.6
icable
Natural
Gas
—
—
—
—

Elec.
0.2
0.1
0.2
0.1

LPG
	
—
—
—

Steam
	
—
—
—

SELF-GENERATED FUELS
Elec.
—

Refinery
Gas
—

Catalytic
Coke
3.2
2.1

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    9
Data Type: 5-PEP
Page 162 of 189
                                 ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
19

20

21

Control
Strategy
Mix
1
2
1
2
1
2
PURCHASED FUEL'S
Coal
—
—
—
—
—

Oil
17.2
11.4
17.2
11.4
22.2
14.7
Natural
Gas
—
—
—
—
—

Elec.
0.6
0.4
0.6
0.4
0.8
0.5
LPG
—
—
—
—
—

Steam
—
—
—
—
—

SELF-GENERATED FUELS
Elec.
—
—
'
—
—

Refinery
Gas
—
—
—
—
—

Catalytic
Coke
1.9
1.3
1.9
1.3
3.4
2.2
CO
0,

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    1
Data Type: 5-PEP
Page 163 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22
23
24
25
Control
Strategy
Mix
1



PURCHASED FUEL'S
Coal
There



Oil
were nc


•
Natural
Gas
refiner



Elec.
ies in R



LPG
igion 1



Steam
.n 1974



SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke


-------
                         FORM  5
                 PRIMARY ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    1
Data Type: 5-PEP
Page 164 of 189
                                  ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
^v
1
2
3
4
5
1
2
3
4
5
1'
2
3
4
5
1
2
3
4
5


•

















PURCHASED FUEL'S
Coal


Regulati


—
—
—
—
—
	
—
—
—
—
—
—
—
—
—
Oil


>ry Scei


—
—
—
—
—
	
—
—
—
—
—
—
—
—
—
Natural
Gas


lario doe


—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Elec.


s not si


2.59
2.59
2.61
2.69
2.74
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


tisfy 19


—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Steam


80 EPA


—
—
—
—
—
	
—
—
—
—
—
—
—
—
—
                                                                     requireme
SELF-GENERATED FUELS
Elec.
its
Refinery
Gas
—
Catalytic
Coke
—
00

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:   Petroleum Refining
Year:       1985
Region:     l
Data Type:  5-PEP
     165 of 189
                                 ALL  UNITS ARE IN 103 Btu/bbl.  Crude Charged

Uegulii tory
Scenario
22




23




2A




25




Control
Strategy
Mix
.1
•• 2
3
A
5 .
1 ^
2
3
A
5 ^
.1
2
3.
A
5 .







•







1
2
3
A
5
PURCHASED FUEL'S
Coal


Regulatt




Uegulati




Regulat


—
—
—
--
--
Oi.l


>ry Scei




>ry Scei




)ry Scei


—
—
—
--
—
Matural
Gas


lario dot




lario doc




ario dot


—
—
—
—
—
Elec.


a not Si




s not s;.




s not sa


2.60
2.60
2.62
2 . 70
2.75
LPC


tiafy EP




tisfy El-1




tisfy EP


—
—
—
—
—
Steam


A 1985




A 1985




v 1985 i


—
—
—
—
—
                                                                      requireme
                                                                      requJ renie
                                                                      equiremer
Sl'LF-Cl'NERATEl) FUK1.S
Elec.
its
its
ts
Refinery
Cay


—
CataLyt (c
Coke


--
CO

-------
                          FORM 5

                  PRIMARY  ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    2
Data Type: 5-PEP
Page 166 of 189
                                  ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1 "
2
3
4
5 .,
1>|
2
3
4
5 ,
!^|
2
3
4
5 j


i












PURCHASED FUEL'S
Coal
—

—
—
—


Exceeds




Exceeds




Exceeds


Oil
—
—
—
—
—


1974 R




1974 R




1974 Re


Natural
Gas
—
—
—
—
—


egulator




egulator




julatory


Elec.
2.71
2.71
2.74
2.86
2.95


f requir




f requir




require


LPG
—
—
—
— •
—


;ments




iments




nents


Steam
—
—
—
—
—















SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

00

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year: 1980
Region:  2
Data Type: 5-PEP
Page 167 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
•\
1 J
2
3 ?
4
5 J
1
2
3
4
5
1
2
3
4
5
1
• 2 .
3
4
5
PURCHASED FUEL'S
Coal


Regulat
requii

	
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Oil


ory see
ements.

—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Natural
Gas


lario do


—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Elec.


;s not s


2.70
2.70
2.73
2.85
2.93
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


itisfy 1'


	
—
—
—
—
	
—
. —
—
—
	
—
—
—
—
Steam


ISO EPA


	
—
—
—
—
	
—
—
—
—
	
—
—
—
—
SELF-GENERATED FUELS
Elec.
—
Refinery
Gas
—
Catalytic
Coke
—
-£)
0

-------
        FORM  5

PRIMARY ENERGY  PENALTY
Industry:   Petroleum Refinine
Year:       M**
Region:     2
Data Type:  5-PEP
Page 168 of  189
                 ALL UNITS ARE  IN  103  Btiu/bbl. Crude  Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 ^
2
3
4
5 „
1 ->
2
3
4
r
1 "I
2
3
4
5 J















1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulatt




Regulate




Regulati


—
—
—
--
—
01.1


ry Seer




ry Scei




>cy Seer


—
—
—
—
—
Natural
Gas


ario doe




ario doe




ario doe


—
—
—
—
—
lil.ec.


s not sa




s not sa




s not sa


2.60
2.60
2.62
2.70
2.75
LPC


tisEy EP




t i s f y E P




;isfy EP/


—
—
—
—
—
Steam


V 1985




\ 1985




1985 r


—
—
—
—
—
                                                      equireinei
                                                      equireme:
                                                     equiremen
SEL
Elec.
us
>ts
IS
F-CKNERATEI)
Refinery
Gas


—
FUELS
Catalytic
Coke


—

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    3
Data Type: 5-PEP
Page 169 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1 "
2
3
4
. 5 ,
*^.
1
2
3
4
5 J
1 ^|
2
3
4
5 .















PURCHASED FUEL'S
Coal

—
—
—
—


Exceeds




Exceeds




Exceeds


Oil

—
—
—
—


1974 R(




1974 Re




1974 Re


Natural
Gas

—
—
—
—


gulatorj




gulatorj




gulator)


Elec.
2.71
2.71
2.74
2.86
2.95


require




require




require


LPG

—
—
—
—


ments




ments




ments


Steam

—
—
—
—















SELF- GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

fb

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    3
Data Type: 5-PEP
Page 170 of 189
                                 ALL  UNITS ARE IN 103  Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 "|
2
3 >
4
5 J
1
2
3
4
5
1
2
3
4
5
• 1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulat


	
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Oil


ory See


	
—
—
—
—
_^
__.
—
—
—
	
—
—
—
—
Natural
Gas


nario do


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Elec.


js not s


2.62
2.62
2.64
2.73
2.79
2.53
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


itisfy 1


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Steam


)80 EPA


—

—
—
—
—
—
—
—
—
—
—
—
—
—
                                                                     requiremt
SELF-GENERATED FUELS
Elec.
nts
Refinery
Gas
—
Catalytic
Coke
—
Ui

-------
                          FORM  5

                 PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1.985
Region:    3
Data Type: 5-PEP
Page 171 of 189  .
                                  ALL UNITS  ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 >,
2
3
4
5
1 "
2
3
4
r
I
2
3
4
5 •>


\


\



J





1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulatt




Regulate




Regulati


—
—
—
—
—
Oil


ry Scei




ry Scei




ry Scei


—
—
—
—
—
Natural
Gas


ario doe




ario doe




ario doe


—
—
—
—
—
IMcc.


s not sa




s not sa




3 not sa


2.60
2 . 60
2.62
2./6
2.75
LPG


tisfy EP




tisCy El1




:lsfy EP/


—
' —
—
—
—
Steam


\ 1985




V 1985




1985 t


—
—
—
—
—

•equircmei
:equ Lreinei
equiremen
SELF-GENERATED FUELS
Elec.
ts
ts
:s
Refinery
Gas


—
Catalytic
Coke


—
-O

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    4
Data Type: 5-PEP
Page 172 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl.  Crude  Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1 ^
2
3
4
5 ^
1 >
2
3
4
5 _,
1 "]
2
3
4
5 „


>












PURCHASED FUEL'S
Coal

—
—
—
—


Exceeds




Exceeds




Exceeds


Oil

—
—
—
—


1974 Re




1974 R«




1974 Re


Natural
Gas

—
—
—
—


gulator}




gulator)




gulator)


Elec.
2.71
2.71
2.74
2.86
2.95


require




require




require


LPG

—
—
—
—


ments




ments




ments


Steam

—
—
—
—















SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

-0

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum  Refining
Year:      1980
Region:    4
Data Type: 5-PEP
Page 173 of 189
                ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 •)
2
3 V
4
5 J
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
PURCHASED FUELS
Coal


Regulate


	
—
—
—
—
	
—
—
—
—
—
—
—
—
—
Oil


ry Scet


	
—
—
—
—
	
—
—
—
—
—
—
—
—
—
Natural
Gas


ario doe


	
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Elec.


s not sa


2.71
2.71
2.74
2.85
2.94
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


tisfy 19


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Steam


50 EPA


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
                                                    requiremei
SELF-GENERATED FUELS
Elec. ,
its
Refinery
Gas
—
Catalytic
Coke
—

-------
        FORM  5
PRIMARY ENERGY  PENALTY
 Industry:   Petroleum Refining
 Year:       1985
 Region:     4
'Data  Type:  5-PEP'
 Page 174  of 189
                 ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 "•
2
3
4
5 _,
1 "
2
3
4
5
i
2
3
4
5 -^


s




>




i


1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulatt




Regulatt




Regulat


—
—
--
—
—
Oil


iry Scei




>ry Scei




jry Scei


—
—
—
—
—
Natural
Cas


ario doc




ario dot:




ario doc


—
—
—
—
—
Elec.


s not sa




s not s;i




s not sa


2.60
2 . 60
2.62
2.70
2.75
LPC


tisfy E'P




tisfy E'P




cisfy EP<


—
—
—
—
—
Steam


\ 1935




i\ 1985




L 1985 i


—
—
—
—
—
                                                      equireme
                                                     ire quir erne
                                                     equiremenus
SELF-GENERATE!) FUELS
Elec.
its
its
US
Refinery
Gas

—
Catalytic
Coke

—

-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:     5
Data Type: 5-PEP
Page 175 of 189
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1 ^
2
3
4
5 „
1 "
2
3
4
5 „
1 "
2
3
4
5 „


•




>







PURCHASED FUEL'S
Coal
	
—
—
—
—


Exceeds




Exceeds




Exceeds


Oil
	
—
—
—
—


1974 R(




1974 R




1974 R


Natural
Gas
—

—
—
— '


igulator)




igulator?




igulator]


Elec.
2.71
2.71
2.74
2.86
2.95


require




require




' requirt


LPG
—
—
—
—
—


ments




ments




ments


Steam
—
—
—
—
—















SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke
•

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum  Refining
Year:      1980
Region:    5
Data TVpe: 5-PEP
Page 176 of 189
                                 ALL  UNITS  ARE IN 103  Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 "")
2
3 >
4
5 J
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulate


—
—
—
—
—
—
—
—
—
—
	
—
—
—
—
Oil


ry Seer


—
—
—
—
—
—
—
—
—
—
	
—
—
—
—
Natural
Gas


ario doe


—
—
—
—
—
—
—
—
—
—
	
—
—
—
—
Elec.


s not sa


2.67
2.67
2.73
2.84
2.92
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


tisfy 19


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Steam


SO EPA


—
—
—
—
—
—
—
—

—
—
—
—
—
—
                                                                     requiremei
SELF-GENERATED FUELS
Elec.
ts
Refinery
Gas
—
Catalytic
Coke
—
-0

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    5
Delta Type: 5-PEP
Page 177 of 189
                                 ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged
fb
8

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 ^
2
3
4
5 ,
1 ~)
2
3
4
5 J


»







1 ]
2
3
4
5 J
.1
2
3
4
5
PURCHASED FUELS
Coal


Regulate




Regulat<




Regulatt


—
—
—
--
—
Oil


ry Scei




ry Scei




iry Scei


—
—
—
—
—
Natural
Gas


ario doe




jiijrio doc




ario doe


—
--
—

—
Elec.


s no t B i\




s not sa




s not sa


2.60
2.60
2.62
2.70
2.75
LIJ0


titify EP




tisfy EF




:lsfy EP/


—
—
—
—
—
Steam


\ 1985




V 1985




. 1985 r


—
—
—
—
--



requiremei




requiremei




SELF-GENERATED FUELS
Elec.


its




its




equirements









—
—
—
—
--
Refinery
Gas















—
—
—
—
—
Catalytic
Coke















—
—
—
—
—

-------
                         FORM 5

                PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    6
Data Type: 5-PEP
Page 178 of 189
                                 ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
22




23




24




25



Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5 ;
I ^
2
3
4
5 ^
1 ^
2 .
3 '
4
5







>






PURCHASED FUEL'S
Coal

—
—
—
—


Exceeds




Exceeds




Exceeds

Oil

—
—
—
—


1974 I




1974 F




1974 F

Natural
Gas

—
—
—
—


egulator




egulator




egulator

Elec.
2.71
2.71
2.74
2.86
2.95


y requir




y requir




y requir

LPG

—
—
—
—


jments




jments



'
jments

Steam

—
—
—
—
' '













SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

o

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:     6
Data Type: 5-PEP
Page 179 of 189
                                 ALL UNITS ARE  IN  103  Btu/bbl.  Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1 ^
2
3 S
4
5 J
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulat


—
—
—
—
—
—
—
—
—
—
	
—
—
—
—
Oil


ory See


—
—
—
—
—
—
—
—
—
—
	
—
—
—
—
Natural
Gas


nario do


—
—
—
—
—
—
—
—
—
—
	
—
—
—
—
Elec.


as not s


2.71
2.71
2.74
2.86
2.95
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


itisfy 1


	
—
—
—
—
	
—
—
—
—
	
—
—
— _
—
Steam


)80 EPA


	
—
—
—
—
j 	
—
—
—
—
	
—
—
—
—
                                                                     requiremc
SELF-GENERATED FUELS
Elec.
nts
Refinery
Gas
—
Catalytic
Coke
—
fc
o

-------
                          FORM  5

                  PRIMARY  ENERGY  PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    6
Data Type: 5-PEP
Page 180 of 139
                                  ALL UNITS ARE IN 103  Btu/bbl.  Crude Charged

Regulatory
Scenario
22




23





24




25




Control
Strategy
Mix
1 ^)
2
3
4
5 .,
1 1
2
3
4
5 ,







»


•x
1
2
3
. 4
5 ^


>


1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulate




Regulate





Regulate


—
—
—
—
—
Oil


ry Scei




ry Scei





>ry Seer


—
—
—
—
—
Natural
Gas


arlo doe




ario doc





ario doe


—
—
—
—
—
Elec.


s not sa




s not sa





s no t s a


2.60
2.60
2.62
2.70
2.75
LPG


Lisfy EP




tisfy EP





Eisfy EPy


—
—
—
—
—
Steam


V 1985




V 1985





k 1985 i


—
—
—
—
—



:ec|uiremei




requireiuei





equlremen







SELF-GENERATED FUELS
Elec.


ts




its





us


—
—
—
—
—
Refinery
Gas
















—
—
—
—
—
Catalytic
Coke
















--
—
—
—
—
8

-------
                         FORM 5

                 PRIMARY ENERGY PENALTY
Industry:
Year:
Region:
Data Type: 5-PEP
Page 131 of 189
Petroleum Refining
1974
7
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2 .
3
.. 4
5
1 ""
2
3
4
5 >
1 "1
2
3
4
5 „
1 ^
2
3
4
5 J







t







PURCHASED FUELS
Coal
—
—
—
—
—


Exceed




Exceed




Exceed


Oil
	
—
—
—
—


; 1974




5 1974




5 1974


Natural
Gas
	
—
—
—
—


legulatoi




lequlatoi




legulatoi


Elec.
2.71
2.71
2.74
2.86
2.95


•y requii




y requii




y requii


LPG
	
—
—
—
—


ements




ements




ements


Steam
	
—
—
—
—















SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

fo
o
-C.

-------
                        FORM 5

                PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    7
Data Type: 5-PEP
Page 182 of 189
                                ALL UNITS ARE  IN  103'Btu/bbl.  Crude  Charged

Regulatory
Scenario
22





23




24




25




Control
Strategy
Mix
1 ^
2
3
4
5
J
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5


S


















PURCHASED FUEL'S
Coal


Regulat



—
—
—
—
—
	
—
—
—
• —
	
—
—
—
—
Oil


Dry See



—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Natural
Gas


lario dot



—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Elec.


:s not s;



2.69
2.69
2.72
2.83
2.92
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


tisfy I1.



—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Steam


80 EPA



—
—
—
—
—
	 	
—
—
—
—
	
—
—
—
' —



requireme


















SELF-GENERATED FUELS
Elec.


its



—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
Refinery
Gas






—
—
.
—
—
	
—
—
—
—
	
—
—
—
—
Catalytic
Coke






—
—
—
—
—
	
—
—
—
—
	
—
—
—
—
a

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:     7
Data Type: 5-PEP
Page 183 of 189
                                 ALL UNITS ARE IN 103 litu/bbl. Crude Charged

Regulatory
Scenario

22



23


24




25




Control
Strategy
Mix
.1 ^
2
3
5 ,
1 "^
2
3
1 "
2
3
A
5 J


•






i


1
2
3
A
5
PURCHASED FUEL'S
Coal



Regulate



Regulati


Regulat


—
—
—
—
—
Oil



>ry Scei



>ry Scei


>ry Scei


—
—
—
—
--
Natural
Gas



ario dot



lario do(


inrio dot


—
—
—
—
—
Elec.



s not Si



s not s;


s not Sii


2.60
2 . 60
2.62
2.70
2.75
1..PG



tisfy El'



tisfy El'


tisfy EP


—
—
—
—
—
Steam



A 1985



A 1985


V 1985 i


—
—
—
—
—





requirenie



requiremc


•equiremer;







SELF-GENERATED FUELS
Elec.



its



its


ts


—
—
—
—
—
Refinery
Gas













—
—
—
—
—
Catalytic
Co Ice













—
—
—
--
—
o

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:    8
Data Type: 5-PEP
Page 184 of 189
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1 ""
2
3
4
5 ,
1 ^
2
3
4
5 .,
1 "
2
3
4
5 _


)




\







PURCHASED FUELS
Coal
. 	
—
—
—
—


Exceeds




Exceeds




Exceeds


Oil
	
—
—
—
—


1974 Re




1974 Rt




1974 R«


Natural
Gas
	
—
—
—
—


gulator>




gulatory




gulator}


Elec.
2.71
2.71
2.74
2.86
2.95


require




require




require


LPG
	
—
—
—
—


ments




ments




ments


Steam
	
—
—
—
—















SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

(b
O

-------
                         FORM 5
                 PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    8
Data Type: 5-PEP
Page 185 of 139
                                 ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario

22




23




24




25




Control
Strategy
Mix
"\
1 ]
2
3 ?
4
5 J
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
PURCHASED FUEL'S
Coal



Regulat


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Oil



>ry Scei


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Natural
Gas



lario doe


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Elec.



s not Sc


2.71
2.71
2.74
2.86
2.95
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG



tisfy 19


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Steam



80 EPA


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
                                                                    requireme
SELF-GENERATED FUELS
Elec.
its
Refinery
Gas
—
Catalytic
Coke
—
fo
CO _

-------
        FORM  5

PRIMARY ENERGY  PENALTY
                                                             Industry:   Petroleum Refining
                                                             Year:       1985
                                                             Region:     ft
                                                             Data Type:  5-PEP
                                                             Page 186  of 189
                                  ALL UNITS  ARE IN 103 Btu/bbl. Crude  Charged
Jb
o

Regulatory
Scenario
22




23



24




25




Control
Strategy
Mix
1^
2
3
4
5 >
.'P
2
3
4
n
2
3
4
5>


'








t


1
2
3
4
5
PURCHASED FUEL'S
Coal


Regula




Regula



Regula


—
—
—
—
—
Oil


•ory Sc(




;ory Sc



tory Sc


—
—
—
--
—
Natural
Gas


mario d(




mario d<



mario dc


—
—
—
—
—
Elec.


es not i




>es not :



es not s


2.60'
2.60
2.62
2.70
2.75
LPG


atisfy !•




atisfy !•



atisfy E


--
—
—
—
—
Steam


PA 1985

>


PA 1985



'A 1985


—
—
—
—
—
                                                                       requirem ^
                                                                       requirem
                                                                       requiremc
SELF-GENERATED FUELS
Eiec.
.ints
nts
Refinery
Gas

—
Catalytic
Coke

—

-------
                        FORM 5

                PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1974
Region:     9
Data Type: 5-PEP
Page 187 of 189
                                ALL  UNITS ARE  IN  103  Btu/bbl.  Crude  Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1^
2
3
4
5 ^
1"
2
3
4
5,
i"!
2
3
4
5 >


•









>


PURCHASED FUEL'S
Coal
	
—
—
—
—


Exceed




Exceed




Exceed:


Oil
__
—
—
—
—


i 1974 1




i 1974 I




; 1974 I


Natural
Gas
__
—
—
—
—


egulatoi




.equlatoi




egulatoi


Elec.
2.71
2.71
2.74
2.86
2.95


y requii




y requii




y requii


LPG
__
—
—
—
—


ements




ements




ements


Steam
__
—
—
—
—















SELF-GENERATED FUELS
Elec.

Refinery
Gas

Catalytic
Coke

o

-------
        FORM 5

PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1980
Region:    9
Data Type: 5-PEP
Page 188 of 189
                ALL  UNITS  ARE IN 103  Btu/bbl. Crude Charged

Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1"|
2
3 ?
4
5 J
1
2
3
4
5
1
2
3
4
.5
1
2
3
4
5
PURCHASED FUEL'S
Coal


Regulat


—
—
—
—
—
—
. —
—
—
—
—
—
—
—
—
Oil


ory See


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Natural
Gas


nario do


—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
Elec.


es not s


2.68
2.68
2.71
2.82
2.90
2.59
2.59
2.61
2.69
2.74
2.60
2.60
2.62
2.70
2.75
LPG


itisfy 1


—
—
—
—
—
—
—
—
—
—
	
—
—
—
—
Steam


)80 EPA


	
—
—
—
—
—
—
—
—
—
	
—
—
—
—
                                                     requireim
SELF-GENERATED FUELS
Elec.
nts
Refinery
Gas
—
Catalytic
Coke


-------
        FORM 5
PRIMARY ENERGY PENALTY
Industry:  Petroleum Refining
Year:      1985
Region:    ^
Data Type: 5-PEP
Page 189 of 139
                ALL UNITS ARE IN 103 Btu/bbl. Crude Charged

Regulatory
Scenario

22




23




24




25




Control
Strategy
Mix
-v
1
2
3
4
5 -
1 ""
2
3
4
5 J







i


M
2
3
4
5j
1
2
3
4
5
PURCHASED FUEL'S
Coal



Regulai




Uegulai




Regula


—
—
—
—
—
Oil



ory Sci




ory Set




ory Sec


—
—
—
—
—
Natural
Cay



nario d(




nario dr.




nario do


—
—
--
—
—
Elec.



es not s




es not s




us not s


2 . 60
2.60
2.62
2.70
2.75
LPG



utisfy E




atisfy E




itisfy El


—
--
—
—
—
Steam



>A 1985




'A 1985




A 1985


—
—
—
—
—


requireiin
requ i renii
requireme
SELF-GENERATED FUELS
Elec.
:nts
,«.
its
Refinery
Gas


—
Catalytic
Coke


—

-------
          FORM 6





Secondary Impact Indicators

-------
                                                DCN 77-100-134-02-02


                                                     Page 1 of 192

	SECONDARY  IMPACT INDICATORS CONTROL EQUIPMENT INDEX	


Index	Control Equipment	
          •Particulates

A (P)     Fluid Catalytic Cracking^unit  (FCC) flue gas rate
          requiring control, in 10s scfm.

B (P)     Number of FCC's requiring control.

C (P)    • Particulate recovery efficiency in weight percent.

D (P)     Recurring ammonia requirement  for Electrostatic  Precip-
          itator (ESP) feed conditioning, in pounds per  hour
          (anhydrous basis).

E (P)     Recurring water make-up requirement for wet scrubbing
          in gallons per minute (GPM)


          S02
A (S)     Additional Distillate Hydrodesulfurization  (HDS)  capacity,
          isi 103 barrels per day  (BPD) .
B (S)     Additional Gas Oil HDS  capacity in 103 BPD.

C (S)     Additional Residual HDS capacity in 103 BPD.
D (S)     Additional capacity to  remove EzS from fuel gas by
          amine absorption, in 10s scfd fuel gas.
E (S)     Additional sulfur recovery capacity (Glaus units),
          in long tons per day (LTPD)

F (S)     Additional Glaus unit tail gas treating capacity  in
          LTPD sulfur.
G (S)     Additional FCC flue gas scrubber capacity in  103
          actual cubic feet per minute  (ACFM).

H (S)     Recurring requirement for HDS catalyst for use  in
          treating middle distillates, in tons per year  (TPY).

I (S)     Recurring requirement for HDS catalyst for gas  oil
          units,  TPY.
J (S)     Recurring requirement for HDS catalyst for residual
          oils, 10Y TPY.

K (S)     Recurring requirement for HDS catalyst for use  in
          tail gas treating operations, TPY.

-------
                                                     Page 2 of 192
 SECONDARY IMPACT INDICATORS CONTROL EQUIPMENT INDEX (continued)

          SO2 (continued)
L (S)     Recurring requirement for amine (probably monoethanol
          amine) in H2S scrubbers, TPY.
M (S)     Recurring requirement for diisopropanol amine for use
          in tail gas treating operations, TPY.
N (S)     Recurring requirement for scrubber liquor for FCC flue
          gas scrubbers, TPY.

          NO*
A (N)     Number of boilers to be constructed with two-stage
          combustion, each of approximately 250 x 10s Btu per
          hour capacity.
B (N)     Number of flue gas recirculation systems to be con-
          structed, each of sufficient capacity to handle a
          250 x 10s Btu per hour boiler.

          Hydrocarbons
A (H)     Additional construction of flares with capacity
          expressed in SCFM.
B (H)     Number of flares to be constructed.
C (H)     Additional pressure tank capacity in 103 barrels.
D (H)     Number of pressure tanks to be constructed.
E (H)     Additional floating roof tank capacity in 10s barrels.
F (H)     Number of floating roof tanks to be constructed.
G (H)     Additional vapor recovery capacity in 103 SCFD.
H (H)     Number of vapor recovery systems to be constructed.
I (H)     Additional covers for API separators with capacity in
          103 GPM of wastewater.
J (H)     Number of covers for API separators to be constructed.

          Lead
A (L)     Additional catalytic reformer capacity in 103 BPD,
          (each reformer will average 15 x 103 BPD).
B (L)     Recurring requirement for reforming catalyst, TPY.
C (L)     Recurring requirement for HDS catalyst, TPY.
D (L)     Additional isomerization capacity in 103 BPD,  (each
        -  unit will average 5 x 103 BPD).
E (L)     Recurring requirement for isomerization catalyst, TPY.

-------
                                                     Page 3 of- 192
 SECONDARY IMPACT INDICATORS CONTROL EQUIPMENT INDEX (continued)

          Lead (continued)
F (L)     Additional alkylation capacity in 103 BPD alkylate,
          (each unit will average 5 x 103 BPD).
G (L)     Recurring requirement for sulfuric acid, TPY.
H (L)     Recurring requirement for hydroflouric acid,  TPY.
I (L)     Recurring requirement for caustic, TPY.
J (L)     Recurring requirement for methylcyclopentadienyl
          manganese tricarbonyl (MMT),  in TPY.
K (L)     Recurring savings in tetraethyl lead consumption in TPY.

          Water
A (W)     Number of wastewater plants controlled at primary
          treatment.
B (W)     Regional capacity of primary treatment plants in 103 GPM.
C (W)     Number of wastewater plants controlled at secondary
          treatment.
D (W)     Regional capacity of secondary treatment plants in
          10Y GPM.
E (W)     Number of wastewater plants controlled at tertiary
          treatment.
F (W)     Regional capacity of tertiary treatment plants in
          10Y GPM.
G (W)     Recurring requirement for activated carbon in TPY.

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Pelroleum Refining
Year:       1974
Region:      1
Daca Type:  6-SI
Page 4    of 192
Regulatory
Scenario
1


2


3


4

I


Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0
0
0
0
0
0
0
0
0
0




B (P)
0
0
0
0
0
0
0
0
0
0




C (P)
___
	 	
	
	
	
	
	
	
	
	




D (P)
0
0
0
0
0
0
o.
0
0
0




E (P)
0
0
0
0
0
0
0
0
0
0










>



•






















































	









-------
                        FORM 6
             SECONDARY IMPACT INDICATORS
Industry:
Year:       1980
Region:    • 1
Delta Type:  6-SI
Page  5  of  192
Petroleum Refining
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125
0.125




B (P)
1
1
1
1
1
1
1
1
1
1




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
8.40
0
0
8.40
0
0
8.40
0
8.40




E (P)
0
0
6.42
0
0
6.42
0
. 0
6.42
6.42










"




































































00

-------
                         FORM 6

             SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     1
Delta Type:  6-SI
Page 6   of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.483
0.483
0.483
0.483
0.483
0.483
0.483
0.483
0.483
0.483




B (P)
5
5
5
5
5
5
5
5
5
5




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (V)
0
32.5
0
0
32.5
0
0
32.5
0
32.5




R CT>)
0
0
24.8
0
0
24.8
0
0
24.8
24.8















































































Qo

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1974
Region:     2
Data Type:  6-SI
Page 7   of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.785
0.785
0.785
0.785
0.785
0.785
0.785
0.785
0.785
0.785




B (P)
10
10
10
10
10
10
10
10
10
10




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (f)
0
52.8
0
0
52.8
0
0
52.8
0
52.8




E-XPJ.
0
0
40.3
0
0
40.3
0
0
40.3
40.3










































































l





-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refitting
Year:       1980
Region:     2
Data Type:  6-SI
Page 8   of 192
Regulatory
Scenario
1


2


3


4



1
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.843
0.843
0.843
0.843
0.843
0.843
0.843
0.843
0.843
0.843




B (P)
10
10
10
10
10
10
10
10
10
10




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (V)
0
56.6
0
0
56.6
0
0
56.6
0
56.6




K (V\
0
0
43.3
0
0
43.3
0
0
43.3
43.3















.




















































	





	



-------
                        FORM 6

             SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1985
Region:      2
Delta Type:  6-SI
Page  9   of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.984
0.984
0.984
0.984
0.984
0.984
0.984
0.984
0.984
0.984




B (P)
10
10
10
10
10
10
10
10
10
10




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
66.1
0
0
66.1
0
0
66.1
0
66.1




E (P)
0
0
50.5
0
0
50.5
0
0 .
50.5
50.5















































































Qj

-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:        1974
Region:       3
Data Type:  6- SI
Page 10   of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.176
0.176
0.176
0.176
0.176
0.176
0.176
0.176
0.176
0.176




B (P)
2
2
2
2
2
2
2
2
2
2




C (P)
0
94. 6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




n (p)
0
11.8
0
0
11.8
0
0
11.8
0
11.8
O



E (P)
0
0
9.04
0
0
9.04
0
0
9.04
9.04















































































Cx)

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      3
Data Type:  6-SI
Page 11   of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.430
0.430
0.430
0.430
0.430
0.430
0.430
0.430
0.430
0.430




B (P)
2
2
2
2
2
2
2
2
2
2




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (V)
0
28.9
0
0
28.9
0
0
28.9
0
28.9




E (P)
0
0
22.1
0
0
22.1
0
0
22.1
22.1



































































	











-------
                         FORM 6
              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1985
Region:      3
Data Type:  6-SI
Page 12   of  192
Regulatory
Scenario
1


2
•

3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.558
0.558
0.558
0.558
0.558
0.558
0.558
0.558
0.558
0.558




B (P)
2
2
2
2
2
2
2
2
2
2




C (P)
0
94.6
90.0
o
94.6
90.0
0
94.6
90.0
99.5




D (7)
0
37.5
0
0
37.5
0
0
37'. 5
0
37.5




E m
0
0
28.7
0
0
28.7
0
0
28.7
28.7

t








*




































































fc

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:
Year:
Region:     4
Data Type: '  6-SI
Page 13  of 192
Petroleum Refining
1974
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2,
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
1.663
1.663
1.663
1.663
1.663
1.663
1.663
1.663
1.663
1.663




B (P)
23
23
23
23
23
23
23
23
23
23




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
*
112.
0
0
112.
0
0
112.
0
112.




E (?)
0
0
85.4
0
0
85.4
0
0
85.4
85.4









































































	





-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:     4
Data Type:  6-SI
Page 14   of 192
Regulatory
Scenario
1


2


3


3




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
1.711
1.711
1.711
1.711
1.711
1.711
1.711
1.711
1.711
1.711




B (V)
23
23
23
23
23
23 .
23
23
23
23




C. (P\
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




n (?)
0
115.
0
0
115.
0
0
115.
0
115.




E (P)
0
0
87.9
0
0
87.9
0
0
87.9
87.9























































.























<0
<0

-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      4
Data Type:  6-SI
Page 15   of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (V)
1.756
1.756
1.756
1.756
1.756
1.756
1.756
1.756
1.756
1.756




B m
23
23
23
23
23
23
23
23
23
23




c (p)
0
94.6
90.0
0
94.6
90.0
0 .
94.6
90.0
99.5




n (P)

118.
—
—
118.
—
—
118.
—
118.




E (V)

—
90.2
—
—
90.2
—
—
90.2
90.2















































































00

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      5
Data Type:  6-SI
Page  16  of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.239
0.239
0.239
0.239
0.239
0.239
0.239
0.239
0.239
0.239




B (P)
4
4
4 .
4 '
4
4
4
4
4
4




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
16.1
0
0
16.1
0
0
16.1
0
16.1




E (P)
0
0
12.3
0
0
12.3
0
0
12.3
12.3
















































































-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:     5
Data Type:  6-SI
                                                          Page 17
         of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P) .
0.315
0.315
0.315
0.315
0.315
0.315
0.315
0.315
0.315
0.315




B (P)
4
4
4
4
4
. 4
4
4
4
4




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (PI
0
21.2
0
0
21.2
0
0
21.2
0
21.2




V. (^
0
0-
16.2
0
0
16.2
0
0
16.2
•16.2




































































	 	 —









o

-------
                         FORM 6
              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      5
Data Type:  6-SI
Page .18   of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.376
0.376
0.376
0.376
0.376
0.376
0.376
0.376
0.376
0.376




R (V}
4
4
4
4
4
4
4
4
4
4




n (p)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (?) .
0
25.3
0
0
25.3
0
0
25.3
0
25.3




R (P)
n
0
19.3
0
0
19.3
0
0
19.3
19.3















































































Go

-------
                         FORM 6
              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      6
Data Type:  6-SI
Page 19   of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508




B (P)
16
16
16
16
16
16
16
16
16
16




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
34.1
0
0
34.1
0
0
34.1
0
.34.1




E (P)
0
0
26.1
0
0
26.1
0
0
26.1
26.1















































































CM

-------
                          FORM 6

               SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:        1980
Region:     6
Data Type:  6-SI
Page 20  of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A m
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508




R m
16
16
16
16
16
16
16
16
16
16




C. fP)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (v)
0
34.1
0
0
34.1
0
0
34.1
0
34.1




E (Y)
0
0
26.1
0
0
26.1
0
0
26.1
26.1

'








s




































































Os)
(x)

-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     6
Data Type:  6-SI
Page 21  of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
. 2
3
' 1




CONTROL EQUIPMENT
A (P)
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508
0.508




B (P)
16
16
16
16
16
16
16
16
16
16




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
34.1
0
0
34.1
0
0
34.1
0
34.1




E (V)
0
0
26.1
0
0
26.1
0
0
26.1
26.1
















































































-------
                         FORM 6
              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      7
Data Type:  6-SI
Page 22   of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
3.863
3.863
3.863
3.863
3.863
3.863
3.863
3.863
3.863
3.863




B (P)
50
50
50
50
50
50
50
50
50
50




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D m
0
259.
0
0
259.
0
0
259.
0
259.




E (P)
0
0
198.
0
0
198.
0
0
1.98.
L98.



























•








































— 	 	









Cu

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      7
Data Type:  6-SI
Page 23   of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A.(P)
4.297
4.297
4.297
4.297
4.297
4.297
4.297
4.297
4.297
4.297




B (P)
50
50
50
50
50
50
50
50
50
50




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




n (p)
.0
289.
0
0
289.
0
0
289.
0
289.



o
E (P)
.0
0
221.
0
0
221.
0
0
221.
221.










































































I





-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Pecroleum Refining
Year:        1985
Region:      7
Data Type:  6-SI
Page  24  of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
5.148
5.148
5.148
5.148
5.148
5.148
5.148
5.148
5.148
5.148




B (V)
50
50
50
50.
50
50
50
50
50
50




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
346.
0
0
346.
0
0
346.
0
346.




E (P)
0
0
264.
0
0
264.
0
0
264.
264.




































































	










-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refilling
Year:       1974
Region:      8
Data Type:  6-SI
Page 25   of  192
Regulatory
Scenario
1


2


3


. 4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.306
0.306
0.306
0.306
0.306
0.306
0.306
0.306
0.306
0.306




B (P)
21
21
21
21
21
21
21
21
21
21




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D (P)
0
20.6
0
0
20.6
0
0
20.6
0
20.6




E m
0
0
15.7
0
15.7
0
0
15.7
0
15.7








































































	
	



Oj

-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:     8
Data Type:  6-SI
Page 26  of  192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.306
0.306
0.306
0.306
0.306
0.306
0.306
0.306
0.306
0.306




B (P)
21
21
21
21
21
21
21
21
21
21




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




1) (V)
0
20.6
*
0
0
20.6
0
0
20.6
0
20. .6




K (V)
0
0
15.7
0
0
15.7
0
0
15.7
15.7







































































	

	



Go

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1935
Region:     8
Data Type:  6-SI
Page 27   of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
0.307
0.307
0.307
0.307
0.307
0.307
0.307
0.307
0.307
0.307




15 (V)
21
21
21
21
21
21
21
21
21
21




C (P^
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




n m
0
20.6
0
0
20.6
0
0
20.6
0
20.6




E (P)
0
0
15.8
0
0
15.8
0
0
15.8
15.8






































































	








-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       .1.9 7/,
Region:      9
Data Type:  6-SI
Page  28  of  192
Regulatory
Scenario
I


2


3


4




Control
Strategy
Mix
1
o
3
.1
2
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
1.102
1.102
1.102
1.102
1.102
1.3.02
1.102
1.102
1.102
1 . 102




B OM
17
17
17
17
17
1.7
17
17
17
17




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




n (PI
0
74.1
0
0
74 . 1
0
0
74.1
0
74. .1




R CP)
0
0
.56.6
0
0
56.6
0
0
56.6
56.6









y





































































-C

-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       i960
Region:      9
Data Type:  6-SI
Page 29   of 192
Regulatory
Scenario
1


2


3


4




Control
Strategy
Mix
1
2
3
1
p
3
1
2
3
1




CONTROL EQUIPMENT
A (P)
1.102
1.102
1.102-
1 . 102
1.102
1.102
1.102
1.102
1.102
1.102




B (P)
17
17
17
17 .
17
17
17
17
17
.17




C (P)
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




n HM
0
74.1
0
0
74.1
0
0
74.1
0
74 . 1




K (V)
0
0
56.6
0
0
56.6
0
0
56.6
56.6










































































, i




^r.

LJ

-------
                         FORM  6
             SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     9
Data Type:  6-ST.
Page 30  of 192
Regulatory
Scenario
1


2


3


4



I
Control
Strategy
Mix
1
2
3
1
2
3
1
2
3
1 .




CONTROL EQUIPMENT
A (P)
1.102
1.102
1.102
1.102
1.102
1.1.02
1 . 102
1.102
1.102
1.102




B (?)
17
17
17
17
17
17 '
17
17
17
17




c m
0
94.6
90.0
0
94.6
90.0
0
94.6
90.0
99.5




D CP)
0
74.1
0
0
74,1
0
0
74.1
0
74.1




E (P)
0
0
56.6
0
0
56.6
0
0
56.6
56.6















































































Gj

-------
                           FORM 6

                SECONDARY IMPACT INDICATIONS
Industry:
Year:
Region:
Data Type:
Page 31  of
Petroleum  Refining
1974
1
6-SI
 192
Rijgnlatoty
Scenario
5




6




7




Control
Strategy
Mix
>
2
3
4
5
1
2
3
4
5
1
2
3
4
5 „








—






CONTROL EQUIPMENT
ACS)






There








BCS)






were r








CCS)






o refii








DCS)

•




eries








ECS)






.n Regi








PCS)






jn 1. ir








CCS)






1974.








HCS)















T.CS)















.TCS)















KC.S)


.












T.(S)















MCS)















NCS)















-c.

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     1
Data Type:  6-SI
Page  32  of 192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1
2
3
4
5
I
2
3
4
5
1
2
3
4
5 ^















CONTROL EQUIPMENT
A(S)






There








BIS)






were n








C(S)






j refir








DTS)

•




eries








R(S)






a Regi








F(S)






>n 1 in








GCS)






1974.








H(S)















I (SO















J(S)















K(S)


.




























M(S)















N(S)
















-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:      1
Data Type:  6-SI
Page 33   of 192
Huguliitory
Scenario
5




6




7




Control
Strategy
Mix
1
2
3 :
4
5
1
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
Am
7.8
7.8
—
—
7.8
7.8
7.8
—
—
7.8
7.8
7.8
—
—
7.8
IUS)
— —
10.5
27.0
37.5
10.5
—
10.5
27.0
37.5
10.5
—
10.5
27.0
37.5
10.5
Cm
	 	
—
—
. —
—
—
—
—
—
—
—
—
—
—
—
Dm
69.1
87.1
111.0
92.9
69.1
92.9
87.1
111.0
92.9
69 . 1
92.9
87.1
111.0
92.9
Em
54.7
73.7
69.1
92.4
77.4
54.7
73.7
69.1
92.4
77.4
54.7
73.7
69.1
92.4
77.4
PCS')

— —
	
92.4
77.4
—
—
—
92.4
77.4
—
—
—
92.4
77.4
cm

	
	
	
240
—
—
—
—
240
—
—
—
—
240
Iim
1.4
1.4
	
	
1.4
1.4
1.4
—
—
1.4
1.4
1.4
—
—
1.4
im

4.0
10.3
14.4
4.0
—
4.0
10.3
14.4
4.0
—
4.0
10.3
14.4
4.0
jm

	
	
. —
	
—
—
—
—
—
—
—
—
—
—
1US}

	 _
. 	 	
2.1
1.8
—
—
—
2.1
1.8
—
• - —
—
2.1
1.8
l,m
31 .6
42.5
39.8
50.6
42.5
3.1.6
42.5
39.8
50.6
42.5
31.6
42.5
39.8
50.6
42.5
M(S}

	
	
16.7
13.9
—
—
—
16.7
13.9
—
—
—
16.7
13.9
Mm

	
	
	
21.9
—
—
—
—
21.9
—
—
—
—
21.9

-------
                           FORM  6

                SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     1
Data Type:  6-SI
Page  34  of 192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1 ^
2
3 J
4
5
1 ^
2
3 J
4
5
1 -^
2 I
3 J
4
5

TTC3T"

Not A

—
7.8

Not A

—
7.8

Not A

—
7.8
B(S)

>plicab

37.5
10.5

jplicab

37.5
6.3

jplicab

37.5
9.4
^isr^

Le

—
—

le

23.8
27.0

le

42.5
47.6
DTS1 1

•

111.0
92.9



277
299



303
319
CONTROL EQUIPMK
E(S)



92.4
77.4



221
249



251
290
i^csr



92.4
77 .4



221
249



251
290



—
240



—
240



—
240
rr
USSZ


—
1.4



—
1.4



—
1.4

T.(S)



14 . 4
4.0



14.4
2.4



14.4
3.6
J(S)



. 0.0
—



2.2
2.5



3.9
4.4
K(S)



2.1
1.8



5.0
5.6



5.7
6.0
US)



50.6
42.5



121
1.36



L38
146
HiS)_



16.7
13.9



79.4
89.1



90.1
95.4
NiSJ_



—
21.9



—
21.9



—
21.9
-c

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     1
Data Type:  6-SI
Page 35  of 192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1 "1
2
3 J
4
5
1 1
2 1
3 J
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S)

Not A

18.6
29.9

Not A

13.9
22.2
29.9
29.9
	
	
29.9
B(S)

iplicab

66.1
20.4

}plicab

66.1
20.4
—
40.6
104
145
40.6
crs)

l.e

34.8
39.5

Le

34.8
39.5
—
	
	
	
—
DTS)
•
•

556
628



527
559
267
359
337
428
359
E(S}



479
520



424
465
211
285
267
357
299
V(S)



406
447



406
447
—
	
	
357
299
crsv



240
240



240
240
—
	
	
—
240
lUS)



15.3
24.6



2.0
4.1
5.5
5.5
	
	
5.5
US)



114
35.3



25.3
7.9
—
15.5
40.0
55.5
15.5
J(S)



•14.3
16.2



3.2
3.6
	
__
	
	
	
K(S}


.
41.2
45.3



9.2
10.1
	
	
	
8.0
6.8
i.rs')



L190
L290



>33
>55
L22
L64
1.54
1.97
1.64
JK£1_


590
682



131
145
	
	
	
64.3
53.8
JUS^



105
249



23.4
55.4
	
	
	 	
	
84.6

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:      1
Data Type:  6-SI
Page 36   of  192
Regnln tory
Scenario
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 >,
2
3 ,
I

4
5
1 >
2
3 .


4
5
CONTROL EQUIPMENT
A(S)

Not A

—
29.9

Not A

—
29.9

Not A

—
29.9
B(S)

jplicab

145
40.6

>plicab

145
24.3

>plicab

145
36.4
cm

le

—
—

Le

91.8
104

Le

164
184
DTS)

•

428
359



1070
1150



1170
1230
ECS}



357
299



854
961



971
1027
PCS')



357
299



•854
961



971
1027
CfSL


—
240



—
240



—
240
1J (S)



—
5.5
,


—
5.5



—
5.5
T (Sl



55.5
15.5



55.5
9.4



55.5
13.8
.im



. —
—



8.4
9.5



15.0
16.8
i> / o \
l\ j Q )

.
8.0
6.8



19.2
21.6



21.9
23.1
US)



197
164



468
526



534
562
M(S)



64.3
53.8



307
344



348
368
N(S)



—
84.6



—
84.6



—
84.6

-------
                           FORM  6

                SECONDARY  IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     2
Data Type:  6-SI
Page 37  of 192
Regulatory
Sr.euorio
5




6




7




Control
Strategy
Mix
i ~)
2
3 J
4
5
1 -,
2
3
4
5 J





1
2
3
4
5
CONTROL EQUIPMENT
ACS')

Not A

3.4
9.6


Not A


9.6
9.6
—
—
9.6
RCS^

iplicah

29.8
8.3


jplicab


—
13.0
33.4
46.4
13.0
c.($}

le

	
	


le


—
—
—
—
—
nrsi

•

119
104





85.5
115
108
137
115
JvOX-


97.6
85.7





67.7
91.2
85.5
114
95.8
V(^



73.4
80.9





—
—
—
114
95.8
C,(^



_ —
240





—
—
—
—
240
IKS}



0.6
1.8





1.8
1.8
—
—
1.8
T^



11.4
3.2





—
5.0
12.8
17.8
5.0
-J-CSX.


	
	





—
	
—
—
—
K(S)



1.6
1.4





	
— —
__
2.6
2.2
i.rs^



54.2
47.8





39.1
52.6
49.2
62.7
52.6
-utei-


13.2
11.1





	
	
	
20.6
17.2
N(frt



	
17.4





__
	
	
	
27.1

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     2
Data Type:  6-SI
Page 37   of 192
Rugiilatciry
Scenario
5




6




7




Control
Strategy
Mix
1 ")
2
3 J
4
5
1 -,
2
3
4
5 J





1
2
3
4
5
CONTROL EQUIPMENT.
A(S^

Not A

3.4
9.6


Not A


9.6
9.6
—
—
9.6
RCS1

iplical

29.8
8.3


iplicab


—
13.0
33.4
46.4
13.0
rr



11.4
3.2





—
5.0
12.8
17.8
5.0
.TCM



	
	





—
—
—
—
—
-KIS1_


.
1.6
1.4





	
	
	
2.6
2.2
T.fS1)



54.2
47.8





39.1
52.6
49.2
62.7
52.6
-MXSX_


13.2
11.1





	
	
	
20.6
17.2
-UCSX-



	
17.4





	
	
	
	
27.1

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     2
Data Type:  6-SI
Page  38  of 192
Regulatory
Scenario
8




9




10




Cunt rol
Strategy
Mix
1 1
2 [
3 J
4
5
1 ^
2
3 J
4
5
1 1
2
3 J
4
5
CONTROL EQUIPMENT
ACS)

Not /i

—
9.6

Not A

—
9.6

Not A

—
9.6
BfS)

pplical

46.4
13.0

pplicat

46.4
7.8

jplical

46.4
11.7
C(S)

le

—
—

le

29.4
33.4

le

52.6
58.9
Dm

•

137
115



342
369



375
395
ECS)



114
95.8



274
308



311
329
PCS)



114
95.8



274
308



311
329
G(S)



—
240



— •
240



—
240
H(S1_


—
1.8



—
1.8



—
1.8
I(S)



17.8
5.0



17.8
3.0



17.8
4.4
J(S)



. —
—



2.7
3.1



4.8
5.4
K(S)



2.6
2.2



6.2
6.9



7.0
7.4
usl


62.7
52.6



150
169



171
180
_M1S3_


20.6
17.2



98.2
110



112
118
JKS)


—
27.1



—
27.1



—
27.1

-------
                           FORM 6

                SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     2
Data Type:  6-SI
Page  39  of 192
Rogulntory
Si:e»\a rlo
5




6




7




Control
Strategy
Mix
1 >
2
3 J
4
5
1 ->
2
>
3 J
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S)

Not A

20.6
52.3

Not A

3.4
4.3
52.3
52.3
—
—
52.3
BCS)

)plicab

153
42.9

aplicab

4.5
1.3
—
70.9
182
253
70.9
CCS)

le

—
—

le

—
—
—
—
—
—
—
DCS)

•

637
564



43.7
41.6
466
627
588
748
627
E(S)



523
462



35.2
31.5
369
497
466
623
522
PCS)



378
317



11.1
9.3
—
—
—
623
522
GTS)



—
240



—
19.9
—
—
—
—
240
J!1SJL_



3.8
9.5



0.6
0.8
9.5
9.5
—
—
9.5
ICS)



58.8
16.5



1.7
0.5
—
27.2
69.8
97.0
27.2
JfS)



. —
—



—
—
—
—
—
—
—
KCS)


,
8.5
7.2



2.5
2.1
—
• —
—
14.0
11.8
LCS)



291
258



20.0
19.0
213
287
268
342
287
_M1S1_


68.1
57.0



2.0
1.7
—
—
—
112
94.0
NCS)


—
89.6



—
2.6
—
—
—
—
148
GJ

-------
                           FORM  6
                SECONDARY  IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     2
Data Type:  6-SI
Page  39  of 192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1 ^
2
3 J
4
5
1 1
2
3 J
4
5
1
2
3
4
5
CONTROL
A(S)

Not A

20.6
52.3

Not A

3.4
4.3
52.3
52.3
—
—
52.3
B7S)

Milicah

153
42.9

iplicab

4.5
1.3
—
70.9
182
253
70.9
C(S)

le

—
—

le

—
—
—
—
—
—
—
D(S)

•

637
564



43.7
41.6
466
627 .
588
748
627
E(S)



523
462



35.2
31.5
369
497
466
623
522
F(S)



378
317



11.1
9.3
—
—
—
623
522
EQUIPMENT
GISL



—
240



—
19.9
—
—
—
—
240
H(S)



3.8
9.5



0.6
0.8
9.5
9.5
—
—
9.5
I (S)



58.8
16.5



1.7
0.5
—
27.2
69.8
97.0
27.2
J(S)



. —
—



—
—
—
—
—
—
—
K(S)


.
8.5
7.2



2.5
2.1
—
• —
—
14.0
11.8
TT(S)



291
258



20.0
19.0
213
287
268
342
287




68.1
57.0



2.0
1 . 7
—
—
—
112
94.0
N \ o )



—
89.6



—
2.6
—
—
—
—
148
-JL.

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     2
Data Type:  6-SI
Page  40  of 192
Ri:gulntocy
Scenario
8




9



10




Control
Strategy
Mix
1 )
2 [
3 J
4
5
1 ^
2
3 J
4
5
1 ^
2 j>
3 J
4
5
CONTROL EQUIPMENT
A(ii)

Not A

—
52.3

Not A

—
52.3

Not A

—
52.3
B(S)

iplicab

253
70.9

)plicab

253
42.5

iplicab

253
63.5
C(S)

le

—
—

le

160
182

Le

287
321
D(S)

•

748
627



1870
2010



2040
2150
E(sy



623
522



1490
1680



1700
1790
PCS)


1
623
522



1490
1680



1700
1790
GfST



—
240



—
240



—
240
11 (S)


—
9.5



—
9.5



—
9.5
-^


97.0
27.2



97.0
16.4



97.0
24.1
J(S)



. —
—



14.6
16.6



26.2
29.3
K(S)

.
14.0
11.8



33.6
37.8



38.2
40.4
SL-


342
287



817
9.19



933
982
M£S-)



112
94.0



536
601



608
644
_mai_


—
148



—
148
-


—
148

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     2
Data Type:  6-SI
Page  41  of 192
Rugul.-itory
Scenario
5




6




7




Control
Strategy
Mix
i 1
2
3 J
4
5
1 •)
2
3 J
4
5
1
2
3
4
5
CONTROL
-~AT3T

Not A

24.7
61.0

Not A

4.1
8.7
61.0
61.0
—
—
61.0


jplicab

176
49.2

)plicab

22.3
6.3
—
82.7
213
295
82.7
C(S)

Le

—
—

le

—
—
—
—
—
—
—
D(S)

•

740
656



103
92.1
544
732
686
873
732
ETST



607
537 ;



84.2
75.2
431
581
544
728
610
F(S)



432
362



55.1
46.1
—
—
—
728
610
EQUIPMENT
G!ST~



—
240



—
34.4
—
—
—
—
240
IKS)



4.5
11.1



0.8
1.6
11.1
11 . 1
—
—
11.1
I(S)



67.3
18.9



8.6
2.4
—
31.7
81.5
113
31.7
J(S)



. —
—



—
—
—
—
—
—
—
K(S)



9.7
8.2



1.2
1.0
—
• —
—
16.4
13.8
US}



338
300



47.0
42.1
249
335
313
399
335
M00_.



78.0
65.3 >



9.9
8.3
—
—
—
131
110
N(S1



—
103



—
13.0
—
—
—
—
172

-------
                            FORM 6

                SECONDARY  IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1935
Region:     2
Data Type:  6-ST
Page  42  of 192
Rugnl atory
Scenario
8




9




10




Control
Strategy
Mix
1 I
2
3 J

[
4
5
1 "I
2
3 J
4
5
1 1
2
3 J
4
5
CONTROL
~ATST~

Not A

—
6.1.0

Not A

—
61.0

Not A

—
61.0
BT31

iplicab

295
82.7

3plicab

295
49.6

iplicab

295
74.2
C(S)

le

—
—

le

187
213

Le

335
375
DTSl^

•

873
732



2180
2350



2390
2510
E(S)



728
610



1740
1960



1980
2090
nrrs)



728
610



1740
1960



1980
2090
EQUIPME
~fe)



—
240



—
240



--
240
W
irrsi



—
11.1
*


—
11.1



—
11.1
KS)



113
31.7



113
19.1



113
28.2
J(S)



. —
—



17.1
19 . 4



30.5
34.2
K(S)



16.4
13.8



39.2
44.1



44.6
47.1
US)



399
335



954
1070



1090
1150
MISI_



131
110



625
702



710
751
N(S)



	
172



—
172



—
172
-J

-------
                            FORM 6

                SECONDARY  IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     3
Data Type:  6-SI
Page 43   of 192
Rugulntory
Scenario
5




6




7




Control
Strategy
Mix
1 1
2 J
3
4
5
1 -s
2
3
4
5 J


—
1
2
3
4
5
CONTKOL EQUIPMENT
Am
Not A

0.5
0.5
0.7


Not A


0.7
0.7
—
—
0.7
B( S)
^plical

0.6
0.9
0.2


>plicab


—
1.0
2.5
3.5
1.0
CCS)
le

—
—
—


le


—
—
—
—
—
nm


6.8
7.4
7.0





6.4
8.6
8.1
10.3
8.6
ECS)


5.4
6.0
5.6





5.1
6.8
6.4
8.6
7.2
V(S~)


—
2.1
2.4





—
—

8.6
7.2
OCR)


—
—
240



i

—
—
—
—
240
HfS^


0.1
0.1
0.1





0.1
0.1
—
—
0.1
1XSJ


0.2
0.3
0.1





—
0.4
1.0
1.3
0.4
.irs^i


—
. —
—





—
—
—
—
—
KfS^


. — _
0.1
0.1





—
• —
—
0.2
0.2
T.rs^


3.1
3.6
3.2





2.9
4.0
3.7
4.7
4.0
-MtSX-

	
0.4
0.3





—
—
—
1.6
1.3
.R(SX_.

__
—
0.5





—
—
—
—
2.0
Oi

-------
                            FORM 6

                 SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     3
Data Type:  6-SI
Page 44   of  192
Hugulntory
Scenario
8




9




10




Control
Strategy
Mix
i 1
2
3 J
4
5
1 ")
2
3 J
4
5
1 ")
2
3 J
4
5
CONTROL EQUIPMENT
A(S)

Not A

—
0.7

Not A

—
0.7

Not A

—
0.7
B(S)

iplicat

3.5
1.0

iplicab

3.5
0.6

jplicab

3.5
0.9
C(S)

le

—
—

le

2.2
2.5

le

3.9
4.4
D(S)

• •

10.3
8.6



25.7
27.7



28.1
29.6
ETST



8.6
7.2



20.5
23.1



23.3
24.7
F(S)



8.6
7.2



20.5
23.1



23.3
24.7
GTS)



	
240



—
240



—
240
M (S)



	
0.1



—
0.1



—
0.1
I(S^



1.3
0.4



1.3
0.4



1.3
0.3
J(S)



. 	
	



0.2
0.2



0.4
0.4
K(S}


.
0.2
0.2



0.5
0.5



0.5
0.6
L(S^



4.7
4.0



11.2
12.6



12.8
13.5
MIS) 	


1.6
1.3



7.4
8.3



8.4
8.9
_Ria)_


	
2.0



—
2.0



—
2.0
03

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     3
Data Type:  6-SI
Page 45  of  192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1 1
2 J
3
4
5
1 1
2 J
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S)
Not A

15.3
15.3
22.4
Not A

9.5
9.5
18.8
22.4
22.4
—
—
22.4
B(S)
iplical:

24.7
' 34.3
5.8
iplicab

32.4
45.0
2.7
—
30.3
78.0
108
30.3
~UT37^
le

—
21.7
24.7
le

—
28.5
32.4
—
—
—
—
—
D(S)

•
216
389
410


175
416
425
200
268
252
320
268
E(S)


171
312
336


150
332
350
158
213
199
267
224
F(S)


—
204
228

%

265
283

—
—
267
224
crsy-


	
	
240


—
—
201
—
—
— .
—
240
H(S)


2.8
2.8
4.1


1.7
1.7
3.4
4.1
4.1
—
—
4.1
T(S)


9.5
13.2
2.2


12.4
17.2
2.9
—
11.6
29.9
41.5
11.6
J (S)


—
• 2.0
2.3


—
2.6
3.0
—
—
—
—
—
KCS)


. —
4.6
5.1


—
6.0
6.7
—

—
6.0
5.1
L(S)


98.7
173
187


83.5
184
194
91.2
123
115
146
123
_MJ£)_

—
72.7
81.6


—
94.8
107
—
—
—
48.1
40.2
.HIS1__

—
—
20.0


—
—
26.4
—
—
—
—
63.2

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     3
Data Type:  6-SI
Page 46  of 192
Regulatory
Sr.enarlo
8




9




10




Control
Strategy
Mix
i "|
2
3 J
4
5
1 >
2 \
3 J
4
5
1 ^
2
3 J
4
5

A(S)

Not A

—
22.4

Not A

—
22.4

Not A

—
22.4
B(S)

pplicat

108
30.3

oplical:

108
18.2

)plicat

108
27.2
C(S)

le

—
—

le

68.6
78.0

le

123
138
CONTROL EQUIPMENT
D(S)

-

320
268





799
862



875
922
ECST^



267
224



638
718



726
768
F(S)



267
224



638
718



726
768
G(S)



—
240



—
240



—
240
H(S)



—
4.1



—
4.1



—
4.1
I(S)



41.5
11.6



41.5
7.0



41.5
10.3
J(S)



. —
—



6.3
7.1



11.2
12.6
K(S}



6.0
5.1



14.4
16.2



16.3
17.3
JL£S1_


146
123



350
393



399
420
M^S1)



48.1
40.2



229
257



260
275
N(S>



—
63.2



—
63.2



—
63.2

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:
Year:
Region:     3
Data Type:  6-SI
Page  47  of  192
Petroleum Refining
1985
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
i "1
2
3 J
4 ••
5
1 1
2
3 J
A
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S)

Not A

16.9
29.1

Not A

4.7
6.7
29.1
29.1
—
—
29.1
IUS)

iplicab

65.5
16.2

iplicab

16.4
8.0
—
39.4
101
14.1
39.4
C(S}

le

37.5
42.6

le

6.4
7.3
—
—
—
—
—
IKS^

•

601
636



130
136
260
349
327 '
416
349
E(S)



479
523



104
111
205
277
259
347
291
pm



348
392



59.4
67.0
—
—
—
347
291
CCS")



—
240



—
55.5
—
—
—
—
240
1 1 ( S )



3.1
5.3



0.8
1.2
5.3
5.3
—
—
5.3
I (SI



25.1
6.3



6.3
3.1
—
15.1
38.9
54.0
15.1
J(S)



• 3.4
3.9



0.6
0.6
—
—
—
—
—
Kf<^


.
7.9
8.8



1.3
1.5
—

—
7.8
6.6
-USX_


266
290



58.0
62.2
119
160
149
190
160
HIS.)



125
141



21.4
24.0
—
—
—
62.5
52.3
_U(S)


—
34.6



—
5.9
—
—
—
—
82.3

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     3
Data Type:  6-SI
Page  48  of 192
Rugulntory
Scenario
8




9




10




Control
Strategy
Mix
1 "1
2 1
3 J
4
5
1 ^
2 r
3 j
4
5
1 "1
2 1
3 J
4
5
CONTROL EQUIPMENT
AfS)

Not A

—
29.1

Not A

—
29.1

Not A

—
29.1
BCS)

•jpllcat

141
39.4

jplicab

141
23.7

jplicab

141
35.4
C(S)

le

—
—

le

89.2
101

le

160
179
Dm

•

416
349



1040
3120



1140
1200
ram



347
291



830
934



944
999
FfSl



347
291



830
934



944
999
fifsl



—
240



—
240



—
240
-1LCSX-



—
5.3



—
5.3



—
5.3
T(S)



54 . 0
15.1



54.0
9.1



54.0
13.4
J(S)



. —
—



8.1
9.3



14.6
16.3
K(S)



6.6



18.7
21.0



21.2
22.5
L( S)



190
-160 	


455
512



519
547
MlS.)_



62.5
-52^3-


298
335



338
358
NTS^



—
82^-3



—
82.3



—
82.3

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     4
Data Type:  6-SI
Page 49  of  192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
i "I
2
3 J
4
5
1 ^
2
3
4
5 J




1
2
3
4
5
CONTROL EQUIPMENT
A(S)

Not A

4.5
15.1


Not A


15.1
15.1
—
—
15.1
B(ST

>plicab

52.3
15.1


>plicab


—
20.5
52.7
73.2
20.5
CCST

le

—
—


Le


—
—
—
—
—
DCS")

•

194
169





135
181
170
217
181
ECS1)



160
140





107
144
135
180
151
FCJJ1)



127
107





—
—
—
180
151
GCS^



. —
240





—
—
—
—
240
IKS')



0.8
2.8





2.8
2.8
—
—
2.8
I (S)



20.0
5.8





—
3.0
20.2
28.1
3.0
J(S')



. —
—





—
—
—
—
—
K(S)



2.9
2.4





—
• —
—
4.1
3.4
T.fS'l



88.6
77.4





61.7
83.0
77.6
98.9
83.0
JUSJ_


22.9
19.2





—
—
—
32.5
27.2
-N-CS-) 	


—
30.2



— . 	
—
—
—
—
42.8

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     4
Data Type:  6-SI
Page 50  of 192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 ^
2
3 J
4
5
1 1
2
3 J
4
5
CONTROL EQUIPMENT
-XT5T~

Not A

—
15.1

Not A

—
15.1

Not A

—
15.1
B(S)

)plical

73.2
20.5

iplicab

73.2
17.8

iplicab

73.2
18.4
C(.S)

le

—
—

Le

46.4
52.7

Le

83.0
93.0
D(S)

•

217
181



540
583



592
623
E(S)



180
151



432
486



491
519
FTS)



180
151 '



432
486



491
519
C(S)



—
240



—
240



--
240
H(S)



—
,2.8



—
2.8.



—
2.8
I(S)



28.1
7.9



28.1
4.7



28.1
7.0
J(S)



. —
—



4.2
4.8



7.6
8.5
K(S)



4.1
3.4



9.7
10.9



11.0
11.7
L(S)


98.9
83.0



237
266



270
284
M(S)



32.5
27.2



155
174



176
186
NTS)


—
42.8



—
42.8



—
42.8

-------
                            FORM 6

                 SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1930
Region:     4
Data Type:  6-SI
Page 51   of  192
RuguJotnry
Scenario
5




6




7




Control
Strategy
Mix
i "I
2
3 \
4
5
1 ^1
2
3 J
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S)

Not A

23.6
78.1

Not A

1.2
2.5
78.1
78.1
—
—
78.1
Tl ( O j
,
iplicab

267
47.5

splicab

5.9
0.9
—
106
272
378
106
C(S)

le

167
190

le

3.7
4.2
—
—
—
—
—
D(S)

•

2160
2320



54.2
57.6
696
937
878
1120
937 .
E(S)



1730
1920



43.2
47.5
551
743
696
931
780
F-TS^



1550
1740



34.5
38.8
—
—
—
931
780
G(S)



—
240



—
240
—
—
—
—
240
rIl(S)



4.3
14.3



0.2
0.5
14.3
14.3
—
—
14.3
T.(S)



102
18.3



2.2
0.4
—
40.6
104
145
40.6
JfS)



• 15.2
17.3



0.3
0.4
—
—
—
	
—
J<1S)_

.
35.0
37.4



0.8
0.9
—

—
20.9
17.7
LfS^



952
1060



24.0
26.3
318
429
401
510
429
MiSl_



559
595



12.4
13.9
—
—
—
168
140
NfS}



—
154



—
3.4
—
—
—
—
221
m.

-------
           FORM 6
SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:    ,   1930
Region:     4
Data Type:  6-SI
Page 52  of 192
Hugulatory
Scenario
8




9




10




Control
Strategy
Mix
1 1
a 1
3 J
4
5
1 •)
2
3 J
4
5
1 1
2
3 J
4
5
CONTROL EQUIPMENT
A(S)

Not A

—
78.1

Not A

—
78.1

Not A

—
78.1
RC
-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:      4
Data Type:  6-SI
Page  53  of  192
Regulatory
Snennrlo
5




6

	 	

7




Control
Strategy
Mix
1 "I

3 J
4
5
1 1
2
3 J
4
5
1
2
3
4
5
CONTROL
ACS)

Not A

39.9
80.5

Not A

0.1
2.4
80.5
80.5
—
—
80.5
B(SY

iplical:

278
'49.6

splicab

11.2
0.5
—
109
280
390
109
C(S)

le

174
198

le

7.0
8.0
—
—
—
—
—
D(S)

•

2240
2410



83.0
89.5
718
965
905
1150
965
E(S)



1790
1991



66.3
74.5
568
766
717
960
804
F(S)



1620
1821



65.4
73.6
—
—
—
960
804
EQUlPMEt
"GTsrn



—
240



—
240 .
—
—
—
—
240
rr
H(S)



4.3
14.7



—
0.4
14.7
14.7
—
—
14.7
~TTST~



107
19.1



4.3
0.8
—
41.8
107
149
41.8

.J1SJ 	


.15.9
18.0



0.6
0.7
—
—
—
—
—
KTS)



36.4
38.9



1.5
1.2
—

—
21.6
18.2
_Lisn



988
1100



36.4
40.7
328
442
413
526
442
Miai_



581
653



23.5
26.4
—
—
—
173
145
N(S5



—
160



—
6.5
—
—
—
—
227

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1935
Region:     4
Data Type:  6-SI
Page  54  of 192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1 4-
2
3 J
4
5
1 1
2
3 J
4
5
1 i
2
3 J
4
5
CONTROL EQUIPMENT
A(S)

Not A

—
80.5

Not A

—
80.5

Not A

—
80.5
BTST

^plicat

390
109

iplicafc

390
65.4

>plicab

390
97.8
C(S)

le

—
—

le

247
280

le

441
495
nm

•

1150
965



2870
2990



3150
3320
E(S)

1

960
804



2300
2580



2610
2760
V(S)
*


960
804



2300
2580



2610
2760
G(S)



—
240



—
240



—
240
nm



—
14.7



—
14.7



—
14.7
T(S)


149
41.8



149
25.2



149
37.2
.TfSl



. —
—



22.5
25.6



40.3
45.1
K(S\


.
21.6
18.2



51.7
58.1



58.8
62.1
r.rs'*



526
442



1260
1410



1440
1510
-JKiO-


173
145



825
926



936
991
_1UJIX-


—
227



—
227



—
227

-------
                           FORM 6

                SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     5
Data Type:  6-SI
Page 55  of  192
Regulatory
Si:ei>orlo
5




6




7




Control
Strategy
Mix
1
2
3
4
5
1 ^
2
3
4
5 ^
\


1
2
3
4
5
CONTROL EQUIPMENT
A(S)
3.4
3.4
—
—
3.4


Not A


3.4
3.4

—
3.4
B(S)
—
6.5
9.8
16.3
6.5


:>plicat


—
6.5
9.8
16.3
6.5
C(S)
—
—
—
—
—


le


—
—
—
—
—
D(S)
26.9
'41.7
33.4
48.2
41.7





26.9
41.7
33.4
48.2'
41.7
E(S)
21.3
33.1
26.5
40.1
34.7





21.3
33.1
26.5
40.1
34.7
F(S)
—
—
—
40.1
34.7





—
—
—
40.1
34.7
T3TS)
—
—
—
—
200





—
—
—
—
200
IKS)
0.6
0.6
—
—
0.6





0.6
0.6
—
—
0.6
US)
—
1.5
3.8
6.2
2.5





—
2.5
3.8
6.2
2.5
J(S)
—
—
—
. —
—





—
—
—
—
—
K(S)
—
—
. —
0.9
0.8





—

—
0.9
0.8
L(S)
4.9
19.1
15.3
22.0
19.1





12.3
19.1
6.1
22.0
19.1
MfS)
—
—
—
7.2
6.3





—
—
—
7.2
6.3
N(S)
—
—
—
7.9





—
—
—
—
7.9
Q

-------
                            FORM 6
                 SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     5
Data Type:  6-SI
Page 56   of  192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1 "1
2
3 J
4
5
1 ^
2 1
3 J
4
5
1 ^
2
3 J
4
5
CONTROL EQUIPMENT
Am

Not A

—
3.4

Not A

—
3.4

Not A

—
3.4
nm

jplicab

16.3
6.5

iplicab

16.3
3.9

)plicab

16.3
5.8
cm

le

—
—

Le

10.3
11.7

Le

18.5
20.7
nm

•

48.2
41.7



120
134



132
143
Km



40.1
34.7



96.0
111



109
119
PCS')



40.1
34.7



96.0
111



109
119
cm



—
200



—
200



—
200
11 m



—
0.6



—
0.6



—
0.6
rm



6.2
2.5



6.2
1.5



6.2
2.2
.im



. —
—



0.9
1.1


•
1.7
1.9
Km



0.9
0.8



2.2
2.5



2.5
2.7
i.m



22.0
19.1



52.6
61.1



60.1
65.3
-tUS}_


7.2
6.3



34.5
40.0



39.1
42.8
-,-RXSX^


—
7.9



—
7.9



—
7.9
--J

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     5
Data Type:  6-SI
Page 57  of 192
Regulatory
Snenarlo
5




6




7




Control
Strategy
Mix
1 ^
2 J
3
4
5
1 1
2 J
3
4
5
1
2
3
4
5
CONTROL
A(S)
Not A

5.3
5.3
24.1
Not A

0.1
o.i
7.3
24.1
24.1
—
—
24.1
IKS)
pplical

57.6
91.1
35.2
jplicat

21.9
' 34.9
13.6
—
46.6
70.2
117
46.6
C(S)
le

—
4.4
5.0
le

—
1.4
1.6
—
—
—
—
—
D(S)

•
267
343
312


84.2
114
102
193
299
240
345
299
E(S)


212
282
258


66.9
94.2
70.1
153
237
190
287
249
T7(S)
•

—
249
225


—
93.9
69.8
—
—
—
287
249
EQUIPMGl


—
—
200


—
—
200
—
—
—
—
200
rr
H(S)


1.0
1.0
4.4


—
—
1.3
4.4
4.4
—
—
4.4
I (S)


22.1
34.9
13.5


8.6
13.4
5.2
—
—
26.9
44 . 7
17.8
J (S)


—
. 0.4
0.5


—
0.1
0.1
—
—
—
—
—
K(S)


—
5.6
5.1


—
2.1
1.9
—
17.8
—
6.5
5.6
L(S)


121
156
143


38.1
51.7
46.5
88.1
137
109
158
137
M(S)


—
52.2
48.5


—
19.3
17.1
—
—
—
51.8
44.8
N(S)


—
—
44.4


—
—
17.1
—
—
—
—
56.9

-------
                           FORM 6

                SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     5
Data Type:  6-SI
Page  58  of 192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 ]
2
3 J
4
5
1 I
2 I'
3 J
4
5
CONTROL EQUIPMENT
ACS}

Not A

—
24.1

Not A

—
24.1

Not A

—
24.1
"lUffT

iplical

117
46.6

iplicab

117
27.9

jplicab

117
41.8
C(S}

le

—
—

le

73.9
84.0

le

132
148
D(S^

•

345
299



860
959



943
1030
E(S)



287
249



688
799



782
854
F(S^



287
249



688
799



782
854
cm



—
200



—
200



—
200
HfS^



—
4'. 4



—
4.4



—
4.4
TCS^



44.7
17.8



44.7
'10.8



44.7
15.9
J(S)



. —
—



6.7
7.7



12.1
13.5
las')



6.5
5.6



15.5
18.0



17.6
19.2
LlS) 	


158
137



377
438



430
468
M£Si_


51.8
44.8



247
286



280
306
N^



—
56.9



—
56.9



—
56.9
Cb

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     5
Data Type:  6-SI
Page  59  of 192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1 1
2 j
3
4
5
* ]
2 J
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
Am
Not A

5.3
5.3
28.9
Not A

—
—
4.8
28.9
28.9
—
—
28.9
nm
)piical

71.5
114
44.5
jplicab

14.3
23.1
9.2
—
55.8
84.0
140
55.8
cm
le

—
4.4
5.0
le

—
—
—
—
—
—
—
—
nm


315
411
371


47.4
68.3
59.1
231
358
287
413
358
Km


249
339
308


37.6
56.9
49.2
183
284
227
344
298
pm


—
305
274


—
56.9
49.2
—
—
—
344
298
om


—
—
200


—
—
200
—
—
—
—
200
vim


1.0
1.0
5.3


—
—
0.9
5.3
5.3
—
—
5.3
im


27.4
43.8
17.0


5.3
8.9
3.5
—
20.9
32.2
53.6
20.9
.im


—
• 0.4
0.5


—
—
—
—
—
—
—
—
Km



6.9
6.2


—
1.3
1.1
—

—
7.7
6.8
_US.X-

142
187
170


21.6
31.2
27.0
106
164
131
189
164
-^L£S)_

—
62.4
57.3


—
10.3
8.9
—
—
—
62.1
53.6
lim_-

—
—
55.6


—
—
16.9
—
—
—
—
68.2

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     5
Data Type:  6-SI
Page  60  of 192
Kugtilntory
Scenario
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 V
2
3 J
4
5
1 1
2-_r
4 .
5
CONTROL
ACS)

Not A

—
28.9

Not A

—
28.9

Not A

—
28.9
BfSl

iplical

140
55.8

:>plical:

140
33.5

)plical:

140
50
con

le

—
—

le

88.5
101

le

158
178
DCSl^

•

413
358



1030
1150



1130
1230
E(S)



344
298



824
957



937
1023
F(S)



344
298



824
957

•

937
1023
EQUIPMENT
C(S)



—
200



—
200



—
200
IKS)




5.3



—
5.3



—
5.3
I (S)



53.6
20.9



53.6
13.2



53.6
19.0
J(S)



—
—



8.1
9.2



14.5
16.2
K(S)



7.7
6.8



18.5
21.5



21.1
23.0
L(S)



189
164



452
524



515
560
BDZj


62.1
53.6



299
343



336
367
JSHZ


—
68.2



—
68.2



—
68.2

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:      6
Data Type:  6-SI
Page  61  of 192
Rugulntory
Scenario
5




6




7




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5 J


»


1
2
3
4
5
CONTROL EQUIPMENT
A(S)
5.5
5.5
—
—
5.5


Not A


5.5
5.5
—
—
5.5
BCS)
—
4.9
21.6
26.5
4.9


iplical


—
4.9
21.6
26.5
4.9
C(S)
—
—
—
—
—


le


—
\
—
—
—
D(S)
52.9
•64.0
67.3
78.4
64.0





52.9
64.0
67.3
78.4
64.0
^nsn
41.9
50.7
54.0
65.3
53.3





41.9
50.7
53.4
65.3
53.3
PCS)
—
—
—
65.3
53.3





—
—
—
65.3
53.3
U(S)
—
—
—
—
272





—
—
—
—
272
H(S)
1.0
1.0
—
—
1.0





1.0
1.0
—
—
1.0
ITS)
—
1.9
8.3
10.2
1.9





—
1.9
8.3
10.2
1.9
-KS)
—
—
—
. —
—





—
—
—
—
—
K(S)
—
—
. —
1.5
1.2





—

—
1.5
1.2
L(S)
24.2
29.3
30.7
35.8
29.3





24.2
29.3
30.7
35.8
29.3
nisi

	
	
11.8
9.6





—
—
—
11.8
9.6
N(S)
	
	
— _
	
17.5





—
—
—
—
17.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:    '   1974
Region:     6
Data Type:   6-SI
Page 62   of 192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1 •)
2
3 J
4
5
1 •)
2
3 J
4
5
1 ^
2
3 J
4
5
CONTROL EQUIPMENT
Af.q)

Not A

—
5.5

Not A

—
5.5

Not A

—
5.5
R(S)

>plicab

26.5
4.9

iplicab

26.5
3.0

>plicab

26.5
4.4
r.(s)

Le

—
—

Le

16.8
19.1

Le

30.1
33.7
D(S)

•

78.4
64.0



196
206



214
220
E(S)



65.3
53.3



156
171



178
183
F(S)



65.3
53.3



156
171



178
183
G(S)



—
272



—
272



—
272
H(S)



—
1.0



—
1.0



—
1.0
irs)



10.2
1.9



10.2
1.1



10.2
1.7
J(S)



. —
—



1.5
1.7



2.7
3.1
KCS)


.
1.5
1.2



3.5
3.9



4.0
4.1
US}



35.8
29.3



85.7
93.8



97.8
100
Mm



11.8
9.6



56.1
61.3



63.7
65.6
_N(S)


—
17.5



—
17.5



—
17.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     6
Data Type:  6-SI
Page  63  of 192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S;
27.4
27.4
—
—
27.4
27.4
27.4
—
—
27.4
27.4
27.4
—
—
27.4
li t S i
	
24.6
108
133
24.6
—
24.6
108
133
24.6
—
24.6
108
133
24.6
C(S )
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
DCS)
265
320
337
392
320
265
320
337
392
320
265
320
337
392
320
E(S)
210
254
270
327
267
210
254
270
327
267
210
254
270
327
267
F(S}
	
—
—
327
267
—
—
—
327
267
—
—
—
327
267
G(S}

—
—
—
272
—
—
—
—
272
—
—
—
—
272
1US1
5.0
5.0
— •
—
5.0
5.0
5.0
—
—
5.0
5.0
5.0
—
—
5.0
1(5)
„_ 	
9.3
41.5
51.0
9.3
—
9.3
41.5
51.0
9.3
—
9.3
41.5
51.0
9.3
JCS^
	
—
—
. —
—
—
—
—
—
—
—
—
—
—
—
-KISX
—
. —
7.4
6.1
—
—
—
7.4
6.1
—
• —
—
7.4
6.1
T.m
121
147
154
179
147
12.1
147
154
179
147
121
147
154
179
147
_M1S)_
—
—
59
48
—
—
—
59
48
—
—
—
59
48
NfS^

—
—
—
87.5
—
—
—
—
87.5
— -
—
—
—
87.5

-------
           FORM 6
SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     6
Data Type:  6-SI
Page  64  of 192
Hugulatory
Scenario
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 1
2
3 J
4
5
1 1
2 1
3 J
4
5

A(S)

Not A

—
27.4

Not A

—
27.4

Not A

—
27.4
BTS}

)plical

133
24.6

jplicab

133
14.8

iplicab

133
22.1
C(S)

le

—
—

le

84
95.5

Le

150
168
-DTST1

•

392
320



978
1030



1.070
1100
CONTROL EQUIPMENT
E(S)



327
267



781
856



889
915
F(S) '



327
267



781
856



889
915
^7 S}



—
212



—
272



—
272
H(S)



—
5.0



—
5.0



—
5.0
TTS)



51.0
9.3



51.0
5.7



51.0
8.4
J(S)



—
—



7.7
8.7



13.7
15.4
K(S)


.
7.4
6.1



17.6
19.3



20.0
20.6
HL(ST



179
147



428
469



489
501
M(S)



59
48



281
307



319
328
N(S1



—
87.5



—
87.5



—
87.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     6
Data Type:  6-SI
Page  65  of 192
Regu In lory
Scenario
5




6




7




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
~srer
27.4
27.4
—
—
27.4
27.4
27.4
—
—
27.4
27.4
27.4
—
—
27.4
BCS^T
—
24.6
108
133
24.6
—
24.6
108
133
24.6
—
24.6
108
133
24.6
C(,S)
—
—
—
—
—
—
—
—
—
—
—
—
—
—
—
D(S)
265
320
337
392
320
265
320
337
392
320
265
320
337
392
320
E(S)
210
254
270
327
267
210
254
270
327
267
210
254
270
327
267
F(S)

—
—
327
267
—
—
—
327
267
—
—
—
327
267
G(S)

—
—
—
272
—
—
—
—
272
—
—
—
—
272
H(S)
5.0
5.0
—
—
5.0
5.0
5.0
—
—
5.0
5.0
5.0
—
—
5.0
KS)

9.3
41.5
51.0
9.3
—
9.3
41.5
51.0
9.3
—
9.3
41.5
51.0
9.3
J(S)

	
	
. —
—
—
—
—
—
—
—
—
—
—
—
K(S)

	
. 	
7.4
6.1
—
—
—
7.4
6.1
—
• —
—
7.4
6.1
US)
121
147
154
179 .
147
121
147
154
179
147
121
147
154
179
147
ncai_

	
	
59
48
—

—
59
48
—
—
—
59
48
N(S)

	
__
—
87.5
—
—
—
—
87.5
—
—
—
—
87.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     6
Data Type:  6-SI
Page 66  of 192
Regulatory
Srenarlo
8




9




10




Control
Strategy
Mix
1 ^
2
3 J
4
5
1 1
2
3 J
4
5
1 ^
2
3 J
4
5
CONTROL EQUIPMENT
A(S)

Not A

—
27.4

Not A

—
27.4

Not A

—
27.4
B(S)

jplicab

133
24.6

jplicab

133
14.8

>plicab

133
22.1
C(S)

le

—
—

ie

84
95.5

le

150
168
D(S)

•

392
320



978
1030



1070
1100
ECS)



327
267



781
856 '



889
915
PTS)



327
267



781
856



889
915
cm



—
272



—
272



—
272
nm



—
5.0



—
5.0



—
5.0
ITS)



51.0
9.3



51
5.7



51
8.4
JfS)



. —
—



7.7
.8.7



13.7
15.4
Km


.
7.4
6.1



17.6
19.3



20
20.6
i,m



179
147



428
469



489
501
Mm



59
48



281
307



319
328
.li(S)


—
87.5



—
87.5



—
87.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:      7
Data Type:  6-SI
Page  67  of 192
Rugiilatory
Scenario
5




6




7




Control
Strategy
Mix
1 I
2
3 J
4
5
1 ^
2
3
4
5 J




1
2
3
4
5
CONTROL EQUIPMENT
A(S;

Not A

5.2
24


Not A


39.9
39.9
—
—
39.9
IKS)

pplicat

146
81.1


jplicaL


—
56.3
137
193
56.. 3
CfS)

le

—
—


le


—
—
—
— v
—
D^

•

492
448





353
477
444
571 '
477
E7S}



401
364





279
378
352
476
397
F7S1



225
188



•

—
—
—
476
397
G(S)



—
236 .





—
—
—
—
237
H ( S }



1.0
4.4





7.3
7.3
—
—
7.3
IfM



55.9
31.1





—
21.6
52.5
74.1
21.6
.Tf<0



—
—





—
—
—
—
—
K(S}


.
5.1
4.2





—

—
10.7
9.0
— L£SX


225
205





161
218
203
261
218
JKS)


40.5
33.7





—
—
—
85.8
71.5
NTTTI !



:
52.4





—
—
—
—
Ill

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     7
Data Type:  6-SI
Page 68  of 192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix

i "|
2
3 J
it
5
1 1
2
3 J
4
5
1 >|
2 I
3

4
5
CONTROL EQUIPMENT
A(S)

Not A

—
39.9

Not A

—
39.9

Not A

—
39.9
B(S)

pplical

193
56.3

jplicat

193
33.8

iplicab

193
50.5
C(S)

le

—
—

le

122
139

le

219
245
D(S)

•

571
477



1420
1530



1560
1640
E(S)



476
397



1140
1280



1300
1330
F(S)



476
397
t


1140
1280



1300
1330
G(S)



—
237



—
237



—
237
H( S)



—
7.3



—
21.6



—
21.6
ifsV



74.1
21.6



74.1
12.5



74.1
19.2
JCS1)



. —
—



11.2
12.7



20
22.4
K(S)


,
10.7
9.0



25.6
28.7



29.2
30.7
T.^



261
218



624
698



712
747
M^



85.8
71.5



409
457



464
478
Nf^



	
111



—
Ill



—
Ill

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     7
Data Type:  6-SI
Page 69  of 192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1 1
2
3 J
4
5
1 -N
2
3 .

[

4
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S)

Not A

23.8
238

Noc A

0.2
38.5
238
238
—
—
>38
B(S)

iplicab

1040
299

jplicab

185
53.4
—
336
817
1150
336
Trrs)

le

18.2
20.7

le

3.1
3.5
—
—
—
—
—
D(S)

•

3400
2920



571
484
2100
2840
2650
3410
2840
E(S)



2820
2420



474
402
1670
2250
2100
2840
2370
F(S}



26 %0
2250



473
401
—
—
—
2840
2370
GfS)

i

—
236



—
236
—
—
—
—
237
nm



4.4
43.5



—
7.0
43.5
43.5
—
—
43.5
l(S)



397
115



69.1
20.5
—
129
313
442
129
JCS^l



• 1.7
1.9



' 0:3
0.3
—
—
—
—
—
KfS)


59.6
51.2



10.6
9.1
—

—
63.8
53.6
T.m



1550
1330



260
221
961
1300
1210
1560
1300
MC
-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:'   Petroleum Refining
Year:       1980
Region:     7
Data Type:   6-SI
Page 70  of 192
Rugulatory
S>:cnarLo
8




9




10




Control
Strategy
Mix

1 ^
2 \
3 J
4
5
1 1
2
3 J


4
5
1 I
2
3 J
4
5
CONTROL
~&T5)

Not A

—
>38

Not A]

—
>38

Not A]

—
^38
B(S)

>plicab

1150
336

>plicab

1150
201

>plicab

1150
30.1
C(S)

Le

—
—

Le

730
830

Le

1310
1460
D(S1

•

3410
2840



8500
9130



mo
)760
E(S)



2840
2370



6790
7600



7720
8130
F(S)



2840
2370



6790
7600



7720
8130
EQUIPME
cTsri



—
237



—
237



—
237
vjT
1 1 ( S )



—
43.5



—
43.5



—
43.5
I(S)



442
129



442
77.6



442
114
JTSI



—
—



66.6
75.7



119
134
K f S )



63.8
53.6



153
171



174
183
US)



1560
1300



3720
4170



4250
4450
M(S)



512
426



2440
2730



2770
2920
NCSl



—
663



—
663



—
663

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     7
Data Type:  6-SI
Page   71 of 192
Rogulntory
Scenario
5




6




7




Control
Strategy
Mix
1 1
2 \
3 J
it
5
1 1
2
3 J
4
5
1
2
3
4
5
CONTROL EQUIPMENT
irtST-

Not A

28
286

Not A

4.1
47.5
186
>86
—
—
'.86
B(S)

jplicab

1250
359

>plicab

210
60.1
—
403
980
1380
403
CCS)

Le

23.6
26.9

Le

5.7
6.5
—
—
—
—
—
D(S)

•

4100
3520



697
603
2520
3410
3180
^.090
3410
E(S)



3390
2920



577
499
2000
2700
2520
3400
2840
FTST



3190
2720



548
470
—
—
—
3400
2840
G(S)



—
236



—
236
—
—
—
—
237
H(S)



5.1
52.1



0.8
8.7
52.1
52.1
—
—
52.1
I(S)



478
137



80.5
23.1
—
154
377
530
154
JfS)



• 2.2
2.5



0.5
0.6
—
—
—
—
—
K(S)


.
71.9
61.7



12.3
10.6
—

—
76.5
64.3
US)



1800
1610



317
275
1.1.50
1560
1450
1870
1560
MfS)



616
533



108
94.9
—
—
—
614
51.1
NTST"



—
910



—
153
—
-,-
—
—
795

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:
Year:
Region:
Data Type:
Page 72   of
Petroleum Refining
1985
7
6- SI
192
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 A
2 i
3 J
4
5
1 4_
2
3 J
4
5
CONTROL EQUIPMENT
A(S)

Not A


286

Not A

—
286

Not A

—
>86
IHST

jplicab

1380
A03

jplicab

1380
242

>plicab

1380
361
C(S)

le

—
—

Le

875
995

Le

1570
1760
nrs1)

•

4090
3410



10200
11000



11200
11700
ECS)



3400
2840 .



8150
9120



9260
9750
F(S)



3400
2840



8150
9120



9260
97bb
GfS)



—
237



—
237



—
237
HfS^



—
52.1



—
52.1



—
52.1
1(5)



530
154



530
93.1



530
137
3(5)



—
—



79.9
90.8



143
160
K(S)


.
76.5
64.3



183
205



209
219
JLXSX-


1870
1560



4460
5000



5100
5340
M(
-------
                           FORM 6
                SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     8
Data Type:  6-SI
Page  73  of 192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1
2
3
4
5
1 .
2
3
4
5 J





1
2
3
4
5
CONTROL EQUIPMENT
A(S)
3.7
3.7
—
—
3.7


Not A


3.7
3.7
—
—
3.7
B(S)
—
6.2
11.7
17.9
6.2


>plicab


—
6.2
11.7
17.9
6.2
TTCSJ^
—
—
—
—
—


I.e


—
—
—
—
—
DCS)
31.0
•45
38.8
52.8
45.0





31.0
45.0
38.8
52.8
45
ECS)
24.6
35.7
30.8
44
37.5





24.6
35.7
30.8
44
37.5
PCS)

—
—
44
37.5





—
—
—
44
37.5
c;cs)

—
—
—
218





—
—
—
—
218
TUSH
0.7
0.7
—
—
0.7





0.7
0.7
—
—
0.7
nrrer

2.4
4.5
6.8
2.4





—
2.4
4.5
6.8
2.4
J(S)

—
—
. —
—





—
—
—
—
—
KC3)

—
. —
1.0
0.9





—

—
1.0
0.9
MS)
14.2
20.6
17.7
24.1
20.6





14.2
20.6
17.7
24.1
20.6
HHJ

—
—
8.0
6.8





—
—
—
7.9
6.8
NTS)

—
	
—
9.5





—
—
—
—
9.5
I

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     8
Data Type:  6-SI
Page  74  of 192
Rogul atory
Scenario
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 •>.
2
'
3 J
4
5
1 ^
2 \
3 J
4
5
CONTROL EQUIPMENT
ACS)

Not A

—
3.7

Not A

—
3.7

Not A

—
3.7
B(S)

jplicab

17.9
6.2

>plicab

17.9
3.7

•plicab

17.9
5.5
CCS)

le

—
—

Le

11.3
12.9

Le

20.2
22.7
D(S)

•

52.8
45



132
138



144.
L47
E(S)



44
37.5



105 .
115



120
123
F(S)

.

44
37.5



105
115



120
.123
GTSI



—
218



—
218



—
218
1US)



—
0.7



—
0.7



—
0.7
US)


6.8
2.4



6.8
1.4



6.8
2.1
.KS1



—
—



1.0
1.2



1.9
2.1
KfS)


.
1.0
0.9



2.4
2.6



2.7
2.8
US}



24.1
20.6



57.7
62.9



65.8
67.2
MfS)



7.9
6.8



37.8
41.2



42.9
44
JUST



—
9.5



—
9.5



—
9.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     8
Data Type:  6-SI
Page  75  of 192
Rugulntory
Scenario
5




6




7
•



Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
^T(ST
18.5
18.5
—
—
18.5
18.5
18.5
—
—
18.5
18.5
18.5
—
—
18.5
B(S)

30.8
58.5
89.5
30.8
—
30.8
58.5
89.5
30.8
—
30.8
58.5
89.5
30.8
C(S)

—
—
—
—
—
—
—
—
—
—
—
—
—
—
D(S)
155
225
194
264
225
155
225
194
264
225
155
225
194
264
225 -
rE(S)
123
179
154
220
188
123
179
154
220
188
123
179
154
220
188
tTSF

—
—
220
188
—
—
—
220
188
—
—
—
220
188
G(S)

—
—
—
218
—
—
—
—
218
—
—
—
—
218
3.4
3.4
—
—
3.4
3.4
3.4
—
—
3.4
3.4
3.4
—
—
3.4
l(S)

11.8
22.4
34.2
11.8
—
11.8
22.4
34.2
11.8
—
11.8
22.4
34.2 •
11.8
J(S)

—
—
. —
—
—
—
—
—
—
—
—
—
—
—
lUS^
—
—

4.9
4.3
—
—
—
4.9
4.3
—

—
4.9
4.3
US')
71
103
88.5
121
103
71
103
88.5
121
103
71
103
88.5
121
103
_tU£I_
—
—
39.7
33.8
—
—
—
39.7
33.8
—
—
—
39.7
33.8
1K£L_
—
—
—
47.5
—
—
—
—
47.5
—
—
—
—
47.5

-------
                           FORM 6

                SECONDARY IMPACT INDICATIONS
Industry:
Year:
Region:     8
Data Type:  6-SI
Page 76  of 192
Petroleum Refining
1980
Regulatory
Scenario
8




9




10




Control
Strategy
Mix
i 1
2
3 J
4
5
1 1
2
3 J
4
5
1 1
2
3 J
4
5
CONTROL EQUIPMENT
AfS1)

Not A

—
18.5

Noc A

—
18.5

Noc A

—
18.5
TUS1*

iplicab

89.5
30.8

jplicab

89.5
3.7

>plicab

89.5
5.5
C.(S)

le

—
—

Le

11.3
12.9

Le

20.2
22.7
_ BIS1
•

264
225



132
138



144
147
Efftt



220
188



105
115



120
123
prs)



220
188



105
115



120
123
cm



—
218



—
218



—
218
IKST



—
3.4



—
3.4



—
3.4
_IXS1_


34.2
11.8



34.2
1.4



34.2
2.1
J(S)



. —
—



: 1.0
1.2



1.9
2.1
Km


.
4.9
4.3



2.4
2.6



2.7
2.8
US}



121
103



57.5
62.9



65.8
67.2
MfS)



39.7
33.8



37.8
41.2



42.9
44.0
_NIS1_


—
47.5



—
47.5



—
47.5
4)

-------
           .FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     8
Data Type:  6-SI
Page  77  of 192
Ki'gtilntoty
Si-.eunrto
5




6




7




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
TCTCT
18.5
18.5
—
—
18.5
18.5
18.5
—
—
18.5
18.5
18.5
—
—
18.5
B(S)
—
'30.8
58.5
89.5
30.8

30.8
58.5
89.5
30.8

30.8
58.5
89.5
30.8
C(S)
—
—
—
—
—
—
•*-
—
—
—
—
—
—
—
—
D(S)
155
225
194
264
225
155
225
194
264
225
155
225
194
264
225
ECS)
123
179
154
220
188
123
179
154
220
188
123
179
154
220
188
F(S)

—
—
220
188
—
—
—
220
188
— .
—
— r
220
188
G(S1

—
—
—
218
—
—
—
—
218
—
—
—
—
218
IKS)
3.4
3.4
—
—
3.4
3.4
3.4
—
—
3.4
3.4
3.4
—
—
3.4
im

11.8
22.4
34.2
11.8
—
11.8
22.4
34.2
11.8
—
11.8
22.4
3.4.2
11.8
JfS)

—
—
. —
—
—
—
—
—
—
—
—
—
—
—
las)
	
—
. —
4.9
4.3
—
—
—
4.9
4.3
—

—
4.9
4.3
i.rs)
71
103
88.5
121
103
71
103
88.5
121
103
71
103
88.5
121
103
Mrs)
__.


	
39.7
33.8
—
—
—
39.7
33.8
—
—
—
39.7
33.8
JKS1_



—
—
47.5
__.
—
—
—
47.5
—
—
—
—
47.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     8
Data Type:  6-SI
Page 78  of 192
lU'gulntory
Suciinrto
8




9




10




Control
Strategy
Mix
1 1
2
3 J
4
5
1 1
2
3 J
4
5
1 1
2 \
3 J
A
5
CONTROL EQUIPMENT
A(S)

Not A

—
18.5

Not A

—
18.5

Not A

—
18.5
BCS)

jplical:

89.5
30.8

)plicab

89.5
3.7

>plicab

89.5
5.5
CTS)

le

—
—

le

11.3
12.9

le

20.2
22.7
D(S)

•

264
225



132
138



144
147
E(S)



220
188



105
115



120
123
F(S)



220
188
•


105
115



120
123
C(S)



—
218



—
218



—
218
H ( S )



—
3.4



—
3.4



—
3.4
KS)



34.2
11.8



34.2
1'.4



34.2
2.1
J(S)



—
—



1.0
1.2



1.9
2.1
K(S)



4.9
4.3



2.4
2.6



2.7
2.8
US)



121
103



57.7
62.9



65.8
67.2
MCST^



39.7
33.8



37.8
41.2



42.9
44.0
N(S)



—
47.5



—
47.5



—
47.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1974
Region:     9
Data Type:  6-SI
Page 79  of 192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1 ^
2 \
3 J
4
5
1 >
2
3
4
5 J


•


1
2
3
4
5
CONTROL EQUIPMENT
A(}^)

Not A

1.2
15.2


Not A


15.2
15.2
—
—
15.2
15 (.S)

iplical

66.7
24.3


>plicab


—
34.9
38.8
73.8
34.9
(J(S)

le

22.4
25.5


le


—
—
—
—
—
1HS)

•

364
369





113
193
139
218
193
E(S)


294
307





89.6
153
110
182
160
F(S)



283
296





—
—
—
182
160
w I O )



—
176





—
—
—
—
176
11 ( S )



0.2
2.8





2.8
2.8
—
—
2.8
KS)



25.6
9.8





—
13.4
14.9
28.3
13.4
J(S)



. 2.1
2-. 3





—
—
—
—
—
K(S)



6.4
6.7





—
	
—
4.1
3.6
US)



159
168





51,7
88.1
63.4
100
88.1
M(S)



88.4
94 . 4





—
—
—
32.8
28.9
N(S)



—
28.0





—
—
—
—
31.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       197A
Region:     9
Data Type:  6-SI
Page  80  of 192
Regulatory
Si:eunrlo
8




9




10




Control
Strategy
Mix
1 1
2
3 J
A
5
1 1
2
3 J
A
5
1 I
2
3 J
A
5
CONTROL EQUIPMENT
A(S)

Not A

—
15.2

Not A

—
15.2.

Not A

—
15.2
IHS)

>plicab

73.8
3A.9

)plicab

73.8
21

jplicab

73.8
31.3
CIS)

Le

—
—

Le

A6.7
53.1

Le

83.6
93.7
D(S)

•

218
193



5AA
577



596
615
E(S)



182
160



A 35
A80



A95
513
F(S)



182
160



A35
A80



A95
513
G(S)



—
176



—
176



—
176
H(S)



—
2.8



—
2.8



—
2.8
KS)



28.3
13. A



28.3
8.1



28.3
11.9
J(S)



. —
—



A. 3
A. 9



7.6
8.6
K(S1_



A.I
3.6



9.8
10.8



11.1
11.5
JL(£1_


100
88.1



238
263



272
281
_MfS^_


32.8
28.9



156
172



177
18A
NfS)



—
31.5



—
31.5



—
31.5

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     9
Data Type:  6-SI
Page  81  of  192
Regulatory
Scenario
5




6




7




Control
Strategy
Mix
1 1
2
3 J
4
5
1 }
2
3 )
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A(S)

Not A

6.1
99

Not A

—
22.8
99
99
—
—
99
B(S)

>plical

449
150

jplicab

110
40.5
—
227
252
479
227
C(S)

le

211
239

le

38.8
44.1
—
—
—
—
—
D(S^

•

2840 ,'
2950



596
606
735
1250
902
1420
1250
ECS)



2283
2456



481
505
582
991
715
1180
1040
F(S)



2247
2420



481
505
—
—
—
1180
1040
GTS)



—
176



—
176
—
—
—
—
176
^HfsT



1.1
18.1



—
4.2
18.1
18.1
—
—
18.1
US)



172
57.6



42.2
15.6
—
86.9
96.6
184
86.9
J(ST



.19.2
21.8



3.5
4.0
—
—
—
—
—
KfST



50.6
54.5



10.8
11.4
—

—
26.5
23.6
US)



1250
1350



264
277
336
572
407
647
572
MCS)


756
821



151
162
—
—
—
213
187
NTST^



—
192



—
47.0
—
—
—
—
205

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1980
Region:     9
Data Type:  6-SI
Page  82  of 192
Itugiilntory
Scenario
8




9




10




Control
Strategy
Mix
1 ]

3 J
4
5
1 ]
2
3 J



4
5
1 1
2
3 J
4
5
CONTROL EQUIPMENT
~RST

Not A

—
99

Not A

—
99

Not A

—
99
BIS)

iplicab

479
227

iplicab

479
136

jplicab

479
203
CTS)

le

—
—

le

303.
345

Le

543
608
D(S)

•

1420
1250



3530
3740



3870
4000
E(S)



1180
1040



2820
3120



3210
3330
FfS)



1180
1040



2820
3120



3210
3330
GfS)



—
176



—
176



—
176
H(S)



—
18.1



—
18.1



—
18.1
im



184
86.9



184
52.4



184
77.3
3(S)



—
—



27.7
31.5



49.5
55.5
K(S)


.
26.5
23.6



63.5
70.2



72.3
74.9
-USX-


647
572



1550
1710



1770
1820
-M1S)__


2.13
187



1010
1120



1150
1190
JUSX—


—
205



—
205



—
205

-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     9
Data Type:  6-SI
Page 83  of  192
Regtil atncy
Scenario
5




6




7




Control
Strategy
Mix
1 1
2
3 J
4
5
1 ^1
2
3 J
4
5
1
2
3
4
5
CONTROL
~T
-------
           FORM 6

SECONDARY IMPACT INDICATIONS
Industry:   Petroleum Refining
Year:       1985
Region:     9
Data Type:  6-SI
Page  84  of  192
Regulatory
Si-.enario
8




9




10




Control
Scrategy
Mix
1 ^
2
3 J
4
5
1 1
2
3 J
4
5.
1 1
2
3 J
4
5
CONTROL EQUIPMENT
A(S}

Not A

—
125

Not A

—
125

Not A

—
L25
R(S}

jplicab

605
286

iplicab

605
172

jplicab

605
257
C(S^

le

—
—

le

383
435

Le

685
768
DCS)

•

1790
1580



4460
4730



4890
5050
RCS^



1490
.1315



3560
3940



4050
4200
pr.
-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1974
Region:     1
Data Type:  6-SI
Page 85  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
•v
1
2
1
2
1
2 J


>









CONTROL EQUIPMENT
A(N) Bfm
0
—


Not Ap[









—
0


licable


























































































































-------
                         FORM 6

              SECONDARY -IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        i960
Region:     i
Data Type:  6-SI
Page 86  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) BM
0
—
2
—
2
—
2
—






—
0
—
2
—
2
—
2


























•



























































































o

-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      1
Data Type:  6-SI
Page 87   of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
—
7
—
7
—
7
—






—
0
—
7
—
7
—
7























































































































-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:     2
Data Type:  6-SI
Page 88  of  192
Regulatory
Scenario
11

12

13

14






i
Control
Strategy
Mix
1
2
1 ^
2
1
2
1
2 .












CONTROL EQUIPMENT
A(N) B(N1
4



Not Apf










4


licable


























































































































-------
                        FORM  6

             SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:     2
Data Type:  6-SI
Page 89  of 192
Regulatory
Scenario
11

12

13

14 ,







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
4
—
5
—
5
—
9
—






—
4
—
5
—
5
—
9











































































































	









r

-------
                        FORM 6
             SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     2
Data Type:  6-SI
Page 90  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
4
—
8
—
8
—
9
—






	
4
—
8
—
8
—
9


























































•



























































8
Oi

-------
                         FORM 6
              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      3
Data Type:  6-SI
Page 91   of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
^
1
2
1
2
1
2


>









CONTROL EQUIPMENT
A(N) B(N)
0
—


Not Ap{









—
0


licable






























•










,















































































0

-------
Industry: Petroleum Refining
SECONDARY IMPACT INDICATORS Year: 1980
Region : 3
Data Type: 6-SI
Page 92 of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
—
3
—
3
—
4
—






—
0
—
3
—
3
—
4























































































































-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region : 3
Data Type: 6- SI
Page 93 of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
—
4
—
4
—
5
—






—
0
—
4
—
4
—
5























































































































-------
                        FORM 6

             SECONDARY 'IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      4
Data Type:  6-SI
Page 94   of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1.
2
1
2


t









CONTROL EQUIPMENT
A(N) B(N)
14
—


Not Ap{









	
14


licable

























































































































D

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industi-y:   Petroleum Refining
Year:       1980
Region:      4
Data Type:  6-SI
Page 95   of  192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
14
—
14
—
14
—
14
—






—
14
—
14
—
14
— "
14





















«
0
































































































-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      4
Data Type:  6-SI
Page  96  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
14
—
14
—
14
—
14
—






—
14
—
14
—
14
—
14














-







































































































Oj

-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      5
Data Type:  6-SI
Page 97   . of 192
Regulatory
Scemirio
11

12

13

14







Control
Strategy
Mix
1
2
1 -,
2
1
2
1
2 >


i









CONTROL EQUIPMENT
A(N) Btm
1
—


Not Ap[









	
1


licable



-





















































































































u

-------
                        FORM 6

             SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:     5
Data Type:  6-SI
Page 98  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
1
	 .
2
—
2
—
4
—






__
1
— .
2 •
—
2
—
4










































































































	 	





1




o

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:
Year:
Region :      5
Data Type:  6-SI
Page  99 of 192
Petroleum Refining
1985
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
1
—
3
—
3
—
5
—






—
1
—
3
—
3
—
5






































-
















































































-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      6
Data Type:  6-SI
Page 100  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1 "1
2
1
2
1
2 ,












CONTROL EQUIPMENT
A(N) B(N)
1
	 „


Not Apf










1


licable


























































































































-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      6
Data Type:  6-SI
Page 101  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
1
—
1
—
1
—
3
—






	 	
1
—
1
—
1
—
3























































































































-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      6
Data Type:  6-SI
Page 102  of  192
Regulatory
Scenario
11

12

13

14







Contr.ol
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
1
__
1
—
1
—
3
—







1
	 	
1
—
1
—
3






-
















































































































-------
                         FORM 6

              SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      7
Data Type:  6-SI
Page 103  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
-^
2
1
2
1
2
**












CONTROL EQUIPMENT ,
A(N) B(N)
0



Not Api










0


licable






























.


























































































CM

-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      7
Data Type:  6-SI
Page 104  of  192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
__
0
_.„
9
—
35
—






__
0
	
0
—
9
—
35















































































































	
>





-------
                          FORM 6

               SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      7
Data Type:  6-SI
Page 105  of 192
Regulatory
Scenario
11

12

13

14
•






Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
	
0
—
15
—
35







	
0
—
0
—
15
—
35










































































































	



	
I




Oi

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      8
Data Type:  6-SI
Page  106 of  192
Regulatory
Scenario
11

12

13

14






1 —
Control
Strategy
Mix
1
2
1
2
1
2
1
2












CONTROL EQUIPMENT
A(N) B(N)
0
—


Not App









	
0


licable
















































































































	








-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:
Year :
Region:
Data Type:  6-SI
Page  107 of 192
Petroleum Refining
1980
8
Regulatory
Scenario
1.1

12

13

14

*





Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
— — .
0
—
0
—
0
—






— .—
0
— —
0
—
0
—
0







































•















































































-------
                          FORM 6
               SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:        1985
Region:     8
Delta Type:  6-SI
Page 108  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) IUN)
0

0
__
0
—
0
—







0
__
L 0
_ —
0
—
0

























o














































































	












GJ

-------
Oi
(b
wm
                         FORM 6
             SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1974
Region:      9
Data Type:  6-SI
Page  109 of  192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1 >
2
1
2
1
2












CONTROL EQUIPMENT
A(N) B(N)
0
—


Not App









	
0


licable
































•

























































































-------
         '  FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:     9
Data Type:  6-SI
Page 110  of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
__
0
	
6
—
13
—







0
— 	
0
	 •
6
—
13























































































































-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      9
Data Type:  6-SI
Page  in of 192
Regulatory
Scenario
11

12

13

14







Control
Strategy
Mix
1
2
1
2
1
2
1
2






CONTROL EQUIPMENT
A(N) B(N)
0
_—
0
—
7
—
14
—






__
0
—
0
—
7
—
14























































































































-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1974
Region:      1
Data Type:  6-SI

Page  112  of 192
Hcguintory
Sccnnrlo
15



16



17



18

Control
Strategy
Hlx
1
2
3
4
1
2
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A fin B (10 C 00 D 00 E 00 V (\i) G (}\) H (H^ T (in T r'H^






> The













~e were r













o refine













ries in 1













egion I













In 1974.








































































	




-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      1
Data Type:  6-SI
Page 113 of 192
ItcRiilntory
Sccnnrl.u
15



16



17



18

Control
Strutcgy
Mix
1
2
3
4
1
2
1
4
1
2
3
/,
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (H) E 00 F OO G (H) H Hn T fl^ J (H)
( Doe<
i
104
Fai
( Doe
j
104
Far
*v
Doe

104
Far
104

not sat

6
exceeds
s not sa

6
exceeds
3 not sa

6
Pvr-pprlp
fi

sfy njiis

155
the reqi
zlsfy th:i

155
the reqi
:isfy thJ

155
t"hp rprn
155

regqlat

25
irements
s recula

25
irements
s regula

25
i rPiT)f>rit •>
?5

i on .

7.1
of this
lion.

7.1
of rli 1s
:ion.

7.1
-of— £hls-
7 1



126
reRulat j


126
regulari


126
eeftul-At-i
12A



33
on.


33
in .


•\-\
HI
33



1



-L--


---
1



3.5



3.5



3 5

3.5



4



4



/,

4













	

-------
           FORM 6
SECONDARY IMPACT INDICATORS  .
Industry:   Petroleum  Refining
Year:       1985
Region:      I
Data Type:  6-ST.
Page 114 of 192
Hngulntory
Scenario
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1

O
CONTROL EQUIPMENT
A (H) B (H) C (H) D (H) E (H) p (,0 G OO H OO I M J H«
( Doe:
J
400
Far
1 Doe;
J
4nn
Far
( Doe:
J
AGO
Fnr
400

> not sat

73
pxrppHs
not sat

•)-\
exceeds
not sat

23
exreeds
23

isfy thi

600
-hf rpqn
isfy thi

600
nhe requ:
i.sfy thi:

600
•he reqiL'
600

regulat

97
rproppt"^
regulat

97
rements
regulat

97
rpmftnts
97

ion.

27.5
nf ]-h-(ft
ion.

27.5
of this
ion

27.5
if f h -\ .q
27.5



490
fPJMll £) M 1


490
regulatit

490
•pjnil «r"f f
490



127
n ±


127
n.


_JL27_
n .
127



6



6



6

6



13.4



-^


13.4

13.4



22



22



22

22
















-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      2
Data Type:  6-SI
Page 115  of 192
Kcgulntory
Scenario
15



16



.17



18

Control
Strategy
Mix
1
7
3
4
1
2
3
4
1
2
3
ti
1

CONTROL. EQUIPMENT
A CHI n cm r cm n cm i? cm i? cm c. cm H cm T tu\ T nn
I Does
j
641
Pnr- (
•v





^

Not i



•
Not /
r

. Not /

not s.'iti

17
ixr.eeds t
pplicab.1



pplicabl


pplicabl

afv this

060
ifi requi

i



^


^

regulat:

1SS
•ementfl <










on.

44
f this r




•







782
^gnifltlpi

.










?01













12













	 34-^_












44


























-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      2
Data Type:  6-SI
Page H6  of 192
Kegulntory
Scoiinrlu
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
?
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (H) E (H.) F (H) G (11) H 00 I OO J OH
I Does
J
700
Far .
I Onpfi
]
700
Far (
I OOPS
J
700
Far <•
700

not satj

40
xceeds t
nnf «aH

40
xceeds t
nor sai-i

40
•xrppHs t-
40

sfy this

1046
lie requi
«fy rVHs

1046
le requli
=;fy rhl'c;

1046
IP rpnirl
1046

regulat:

169
•ements c
-regulaU
169
ements c
rponl n f i

169
PniPn'"'^ n
169

on.

48
f this r
nn .

48
f this r
nn

48
f this r<
48



716
^gulatipi


716
ignl atloi


716
;g«Latio4
7.16



221



221



??1

221



14



14



14

14



36.9



36.9



36 q

36. q



50



50



^0

sn
















-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1985
Region:       2
Data Type:  6-SI
Page  117 of 192
Regulatory
Scenario
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
9
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (H) E (H) F (H) G (II) H (tt) I (M J HO
I Does
j
816
Far e
I Does
j
816
F*r
1 Does
]
816
Far
816

not sati

47
Kceeds t
10 t S?lfl;

47
'xrpprls 1
not satu

47
ixceeds t
47

fy this

1220
e requii
fy this

1220
hp rpqni
sfy this

1990
he requi
1220

regulati

197
ements o
rpgnl at 1 1

197
"fiD^nfR '
reRulat

1^7
rements c
197

)n.

56.0
r this rt
in -

56.0
f this i
on.

56.0
f this r
56.0



995
gulation


995
^-Gulatio


995
^ulatlo
995



258



958



258

95H _



18



1ft



18

1ft



39.4



T) 4



39.4

-— -


sr>



S6



56

56
















-------
                       FORM  6

            SECONDARY  IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1974
Region:     3
Data Type:  6-SI
Page 118 of  192
Uep.ulntory
Scenario
15



16



17



13

Control
Strategy
Mix
1
2
3
4
1
2
•\
/,
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C 00 D W R OH F dO G (H) H (H) I (H) J OO
110
>*
' Far (
S
V
Not /

S
V
( Not ,A


N"t A

13

xceeds t


pplirahl



ppllo.ahl




165

le reqiil


i








27

en)Pnl"-S f











0

f t-Mft r











0

on! f\ f\ nr











0













0













0













0



























00
CO
(x)

-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1980
Region:      3
Data Type:  6-SI
Page 119  of 192
lte|>tilnt:ory
Scenario
15



16



17



18

Control
Strategy
Mix
1
2
3
A
1
2

A
1
2
3



CONTROL EQUIPMENT
A an B an c an D an E an F an r, an H an T an .1 an
279
^
}_^
279
N.
f Far
J
279
>|
[ Far

279

24

,

24

^

24



24

417

h^ requl

417

IIP T-pmrf

417

h/^ ypniH
III 	 l-r_ 1(1.1 i
417

67



67



67



67

0

if—tliis—x

0

F...rhJ« r

19

f Hyic; r

19

0

/iitiil ,aiid-Q

0

^gula-tio
341

-"» V*\\ \_Q_ t "I A

341

0



0



0



RR

0



0



0



6

0



0



0



11 6

0



0



0



34
















-------
                       FORM  6

            SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1985
Region:       3
Data Type:  6-SI
Page 120  of  192
HoRulntory
Scciinr lo
15



16



17



18

Control
Strategy
Mix
1
2
3
f.
I
2
3
A
1
2
3
4
1

CONTROL EQUIPMENT
A no B an c an n on K an T? on n nn u AI\ i an .T a^
368
\
•-^
368
-\
Far

368
>
' Far

368

29

QXGGGclS

29

ixcpeds t

29

:xceeds t

29

551



551

lie rpqni

551

lie requi

551

89



89

rprnfnt-fi i

89

rements c

R9

0

f t- }i -( n ;

0

,f rhis T

25.2

f this r

?5.?

n


egulatio!
0
•
P£ii1 a(-1 n

449

iRulatio

449

n


i •
0

i ,

0



—
n



0



0



40

n



0



0



0

Q



0



0



n















CO
Oj
Oi

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      4
Data Type:  6-SI
Page 121  of 192
Hop.iilntory
Sccunrio
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
?
1
/,
1
2
1
/,
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (II) E (11) F (II) G 01) H on T (n\ T Cm
"v
Does
s
im?
\
Not


X
Not


Not


not sat

Sfl

^pplicab



Vpplicab


Vpplicab


sfy this

— mo_
e.



e.


e .


regulat

244











ton.

49.1













ft?9













•^?n













24













55













72

























-------
                        FORM 6

             SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1930
Region:      4
Data Type:  6-SI
Page 122  of 192
Uep.ulntory
Scenario
15



16



17



18

Control
Strategy
Mix
1
2
3
/,
1
2
1
4
1
2
3
/.
1

CONTROL EQUIPMENT
A (H) B (H) C (11) D (11) E (H) ' V fin fi (u\ H (H) I (H) J (H)
S
Does
j
1045
•x
Does

1045
x
( Does
s
104S
1045


not sat:i

60

not sati

60

not sati

fif)
60


sfv this

1618

sfv this

1638

sfy this

168^
1683


regulat:

?52

regnl n tA
252

refill afi

?S?
252


on.

8S7

on.

857

on .

ftS7
857




50.8



50.8



SO ft
50.8




330



330



330
330




26



26



?fi
26




56



56



S6
56




80



80



80















(»

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     A
Data Type:  6-SI
Page 123  of 192
Hegulntory
Scenario
15



16



17



18

Control
Strategy
Mix
1
?
1
4
1
2
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (11) C OO D (H) E (H) F (H) G OO H OO I 00 J (H)

' Does

1076
•s
> Does

1076

Does
./
1076
. 1076


not sat:

61

not sat:

61

not sat:

61
61


—
1688

sfy this

16R8

sfy this

1688
1688


regular

260

regulat

260
regulat:
260
260


on.

52.2

.on.

52.2

on.

52.2
52.2




881



881



881
881




340



-^


340
340




28



28



28
28




36



36



36
36




86



86



86
86
















-------
                       FORM  6

            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      5
Data Type:  6-SI
Page 124  of 192
Ue[>ulatory
Sconnrlo
15



16



17

9

18

Control
Strategy
Mix

2
•\
4
1
?
3
4
1
2
-\
t,
I

CONTROL EQUIPMENT
A (B) B (H) C (H) D (11) E (H) F fin fi (^ H fHl T (^ T nn
1 Does
j
225
Far t
X
Nnf ^


s
Not ^


Not A

not sati

13
xceeds t

liplicab-1


pplir.fihl


•>pl i f-ahl

sfv this

592
le requii










regulati

54
ements o










on.

11.7
E this r












IQQ
gtilnt lor












71













7













12.3













in

























OJ

-------
                       FORM  6


            SECONDARY IMPACT INDICATORS
Industry:   Petiroleutn Refining

Year:       1930

Region:     5

Data Type:  6-SI

Page 125 of  192
Heftiilntory
Sccnnr l.o
15



16



17



18

Control -
Strategy
Mix
1
2
3
4
1
2
3
A
1
?
3
4
i

CONTROL EQUIPMENT
A (H) B on c on D on E on F on c on H nn
[ Does
j
322
Far (
I HOP'S
j
322
Far <
I Does
j
322
Far (
322

not sati

19
xrpp.ds t
n ' » t - s a. 1 1

19
xr^fifl.q r
not sat:!
19
xreeds r
19

sfy tills

ftfift
IP rpqii'l
•sfv this

848
IP rpniii
sfy this

848
le reqnl
848

reRulati

7ft
•pmpnrs r
•tegxi-l^iti
7ft
Ptnppfc; r
rp.i'iilafl

78
emppl'S n
78

on .

16,7
f rMp r
on

16.7
f l-lvls r
nn .

16.7
f 1-lHs r
16.7



7ftS
• fill a t~ 1 ni


285
»pnl Af 1 ni


285
•f»iil af Inr
285



in?



102



102

102



10



10



10

10

_j_mx_

15-1)



15.5



15.5

15.5

J (H1*


4?



42



42

4?















U)
 r-

-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:        1985
Region:      5
Data Type:  6-SI
Page  126 of 192
Hop.ulntory
Sccnnr lo
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
.1

CONTROL EQUIPMENT
A (ii) B (ii) c (ii) D (ii) E (ID F (in n nn H ^n i (H) J (H)
( Does
\
386
Far e
I POPS
\
386
Far e
.LjDnas_
386
Far e
386

not sati

22
tceeds tl
lot 	 aa±i:
22
cceeds tl
10 1" fial~i.c

22
:ceeds tl
22

fy this

102ft
e requir
fy rhls

1020
e requir
Fy t-hTg
1020
e requir
1020

regulati

n.
«
20
this rt
n .

?0
this re
n

20
this re
20



341
gul.ac.l-Qo

341
jitil at ion


34.1
»ulatipn
3il



122



122



122

1??



11



11



11

11



12.9



12 0



12.9

12.9



46



46



46

46
















-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      6
Data Type:  6-SI
Page  127 of  192
HoRiilntory
Scennrlo
15



16



17



18

Control
Strategy
Mix
1
2
3 '
4
.1
9.

t.
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (H) E 00 P OO G (H\ H (n\ T (n\ T fv,\
Does
366
1 Far t
j
N
^ Nnf A


N
Nnf- A


Nol- A

not sati
21
xceeds t


[iplicabl


ipl i rqbl'


plical>l<.

ify this
575
le requii











regulati
88
ements o











>n.
17 . 8
C this r(












300
culation












116













.1.4













0













0


























-c

-------
                        FORM 6 •
             SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      6
Data Type:  6-SI
Page  128 of 192
UcRiilntnry
Scenario
15



16



17



18

Control
StrutcRy
Mix
1
2
3
4
I
2
3
/,
1
2
3
/.
1

CONTROL fcQUIL'MENT
A (H) B (H) C (II) D (H) E (H) F 00 G OH H OM I M J HH
Does i
366
I Far e>
]
Does r
366
I Far PV
J
Does n
366
I Far ex
J
366

ot satis
21
ceeds th

ot satis
21
fpf>r|<5 l-h

ot satis
21
oeedu— th
21

fy this i
57S
j require

:y J:hls. i
57 S
;— xaq.uirx
:y this i
575
:— r-eq-uitt
575

egulatio
88
ments of

88
meats— &£
egulatio
88
iiiaivt^— o.f
88

i .
17.8
this re.i

i .
17.8
-ttiiK— eet
i.
17,8
-thls_r-ei
17.8


inn
ulflMnn -


inn
u-la-feiott-

3ttO
ulation.
300


116



116



	 1J_6__

116


]4



I/,



1/i


1A


0



o



0


19.9


n



Q



n


42










	



Co
-c

-------
                        FORM 6

             SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1985
Region:     6
Data Type:  6-ST.
Page 129  of 192
Regulntory
Secnnr lo
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
/,
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (Hi E (H) F (VI) G (\\) H (») T fu\ J (11)
Does i
366
( Far e->
j
Does r
3^6
I Far ex

Does n
366
I Far ex
J
366

ot satis
21
ceeds th

ot satis
21
rpprls rh

)f satis
21
^pprls rli

21

:y this i
575
i require

:v this i
575
> rfrini re

:v this r
sys
rf-f|ii1 rf

575

esulatlo
8ft
nents of

ejMil atin
88
ments o£
egiilatip
88


88

i.
17.8
this rej

i.

i .
- ^
~^"^ j. tj.j
17.8


3nn
ulation .


- 300
ula-tion-.

300
uXatAoft,
300


116



116



116
»

116


1A



-U



14


14


0



o



n


— 12-^-

o



0



0


42















03
 r-

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       19M
Region:      7
Data Type:  o-SI
Page 130  of 192
Il«p,ulntory
Scenario
15



16



17



18

Control
Strategy
Mix
1
2
1
4
1
9
3
4
1
2
3
4
1

CONTROL 'EQUIPMENT
A an B an c *in n cm K nn F (H) c do H (in i on j (in
I Does i
j
2670
Far e>

Not Af



Not Aj

J
Not Ap

ot satis

152
ceeds th

plicable



plicable


)licable

Ey this :

7020
J requlri










ef-ulatic

644
inents of










i.

138
this re












2354
ill aripn .












844













50













145













182


























-------
                        FORM 6
             SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      7
Data Type:  6-SI
Page  131 of 192
Kegulntory
Scenario
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (11) E (11) F (H) G M H HH T OM .T rm
[ Does i
I
3184
Far e>
I Does r:
1
3184
Far fix
I Does n
J 1
3184
Far ex
3184

ot satis

181
ceeds th
ot satis

181
reer]s rhi
at satis

]ftl
:eeds th
181

fry this i

8370
i require
:y this i

8370
' rpqin'rt-
:y this i

ft3?n
require
8370

enulatio

768
ments of
egnl af'in

lnpn^c; nf
eRulatio

	 7.6.8 	
nents of
768

i.

164.8
this rej
i .

164.8
-this refc
i.

164 8
this re^
1 64 . R



2810
Mlatipn.


2810
ulatioo.

2810
ulation.
2810



1010



1010


1010

10] 0



63



63



63

63



162



162



162

16?



224



224



224

"yyL















01

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      7
Data Type:  6-SI
Page  132 of 192
Hogulntory
Scenario
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B 00 C (H) D .00 E 00 F 00 G OO H OO T fin T rm
Does i

3819
Far e)
1 Does i
J
•*ftlQ
Far e>
I Does r
J
3«1<1
Far ex
3819

ot satis

217
ceeds th
ot satis

217
ceeds th
ot satis

	 Z17_
ceeds th
217

fy this

]0,040
e requin
fy this i

10 040
i require
:v this i

Ifl+MQ-
: require
10,040

egulatic

921
ments of
egu]atio

92]
ments of
egulatio

921
ments of
921

n.

197
this re
i .

197
this re;
ir

197
this rej
197



3365
.ulation.


3365
ulation.


1365
ulation.
3365



1210



i?in



	 1210-
1210



78



-"-


78

7R



128



	 12&_


128

128



272



	 2-7-2-—


272

-^-













•

-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:         1974
Region:      8
Data Type:  6-SI
     133  of 192
Hepulntory
ScRiinrlo
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (H) E (H) F On G HH H (M T M T HH
Does i

247 .
	 F.ar_ej
x
Not AI



Not Ap


Not Ap

ot satis

14
r.efids th

plicable



pllcable


ilicable
	
Cy this :

613
i rpqijl r<










egulatio

60
mfinfs nf










\.

12.?
f-hlfi rpi












90S
nl a M' nn












78












•
IS













13.4













33




















	




-------
                       FORM 6
            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      8
Data Type:  6-SI
Page 134  of 192
UcRiilntory
Sccnnrlo
15



16



17



18

Control
Strategy
Mix
1
2
3
4
1
2
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A CH) B cm c on n cm E cm F cm c, cm H cm T cm T no
I Does i
j
247
Far ej
, nnf.q r

247
Far e>
)Does r

247
Far ex
247

ot satis

14
ceeds th
nf ft»fift

14
ceeds th
ot satis

14
ceeds th
14

Ey this

611
[2 require
fy this i

613
; requin
:v this i

6.13
i requirt
613

eRulatic

60
ments of
pf>nl a f 1 n

60
ments of
egulatlo

60
me n t s of
60

n.

199
r.hi«5 re
)

12.2
this re;
\r

12.2
J:Ms re.}
] 9 9



205
nl atinn .


205
ulation.


90S
90S



78



78



7H

7«



15



15



,.

15



13.4



13.4



13 A

	 ia^i_


33



33



33

33















Gi

-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industi-y:   Petroleum  Refining
Year:       1985
Region:      8
Daca Type:  6-SI
Page 135  of 192
Hcgulntory
Sccunrio
15



16



17



18

Control
Strategy
Mix
1
2
3
4 '
.1.
2
3
4
1
?
3
4
.1

CONTROL EQUIPMENT
A (H) B (H) C (H) D 00 H 00 F OO C. OH H HH T fi-H r cm
Does n

?47
Far ex
'
Does n<

247
Far ex(
Does ri<

247
Far ex i
247

>t satisi

.14
eeds the
1
C S3t;lraf

14
eeds the
t satisf

14
eeds the
14

y this r

6.13
require
y rhis n

fill
requlrei
r fills ri

61.3
reciuirei
613

eu.latloi

60
tents of
' i> 1 1 1 ;\ f i n i

60
ients of
g(il flf1 nn

60
ents of
60



12.2
this reg


12 2
Lhis reg


12,2
:his reg
12 2



205
ilatlon .

-
205
ilat inn.


205
lac ion.
205



78



-^


7ft

78



15



1 S



is

15



1.3.4



13.4



13.4

ft "\



33



33



33

Vt














•
Co

-------
                        FORM 6

             SECONDARY IMPACT INDICATORS
Industry: •  Petroleum  Refining
Year:        1974
Region:      9
Dc\ta Type:  6-SI
Page 136 of 192
Kegulntory
Scenario
15



16 .



17



18

Control
Strategy
Mix
]
?
3
4
1
2
3
/,
1
2 '
3
A
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D (H) E (H) F (H) G (H) H (II) I (H) J (II)
I Does
J
1019
Far e

Not A



Not A


Not A

lot snti

58
xceeds t

pplicabl



}plicabl


>p.licabl(,

fv this

1300
ie requir










reeulat I

246
ements o










m.

69.9
: this rt












1243
eulation












322













32













55.5













11.6

























oo
01

-------
                       FORM  6

            SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      9
Data Type:  6-SI
Page 137 of 192
Regulatory
Scenario
15



16



17



18

Control
Strategy
Mix
•1
2
3
it
1
2
3
it
I
2
3
/,
1

CONTROL EQUIPMENT
A (H) B (H) C (H) D 00 E (11) F (H) G (H) H (H) I (H) J (11)
( Does i
j
1320
Far e>
( Does i
J
1320
Far e>
[ Does v
J 1
1320
Far ex
1320

ot satis

75
ce.eds th
ot satis

75
ceeds th
ot satis

75
ceeds th
75

fy this i

1690
> require
:y this i

1690
; require
:y this i

-JA2Q-L-
; requin
1690

egulatio

319
menrs of
egulatio

319
ments of
egulatio

319
ments of
319

\.

90.8
this rei
i.

90.8
this rej
i.

90.8
this re
90.8



1615
ulatlon.


1615
ul.atioo.


1615
ulation.
1615



418



418



418

418



41



41



41

41



65.7



65.7



65.7

65.7



144



144



144

144














•
VJO
 *

-------
                        FORM 6

             SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:        1.985
Region:      9
Data Type:  6-SI
Page  138 of  192
Hegulntory
Sccnnrlo
15



16



17



18

Control
Strategy
Mix
1
?
3
4
1.
2
3
4
1
2
3
4
1

CONTROL EQUIPMENT
A (H) B (H) C (11) D (H) E (H) F (11) G (11) H (11) I (H) J (11)
Does n

1671
Far ex
Hnpft 11

1671
Far ex
Dnps 11

1671
Far exi
1671

>t satis1

95
teeds the
It e; M I- i « I

95
:eeds the
i r K n 1 1 <4 1

95
eeds the
95

v this r

2130
reoiii re
y Hi I ^ r

2130
require
v I" h 1 j»iil ;i f'l ni

nents of
>fiil n I'i AI

403
tents of
403



114.5
(:his ret


114.5
this reg


114 . 5
this ree
114.5



2037
.il af.ion ,


2037
ilation.


2037
ilation.
?037



528



528



528
'
528



51



51



51

51



56



56



56

56



174



174



174

.174















Gl
a

-------
                      FORM  6

           SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:     1
Data Type:  6-SI
Page 139  of  192
Regulatory
Scenario
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (LJ B (L) C (L) D (L) E (L) F (L) G (1.) H fM T (1* T m K (1.)








> There













were no













ser.ondai













y imnafr













« 1p 1Q7




























































































	

(A

-------
                        FORM 6
             SECONDARY IMPACT INDICATORS
Industry:   Petroleum  R'.fining
Year:       1980
Region:      1
Data Type:  6-SI
Page 140  of . 192
Ucgulntory
Sccnnrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (I,) C (L) D (L) E (U F (L) G (L) H (L) I (L) -T fU K m
0
0
0
0
BNot A









0
0
0
0
liplicabl








0
0
0
0










0.7
0.5
3.8
2.5










0.3
0.2
1.6
1.1
*









1 .8
1.2
3.5
2.3










4.2
2.8
8. -3
5.5










38
25
71
47










53
35
103
68










0
98
n
97










2.5
4 n
4.0










CM
cn

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1985
Region':     1
Data Type:  6-SI
Page  141 of  192
UeRulntory
Scuitnr lo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (U F (U G (L) H (1.) 1 (O -I (LI
24i5
16.2
24.5
16.2
24.5
16.2








16.2
10.7
16.2
10.7
16 . 2
10.7








8.1
5.3
8.1
5.3
8.1
5.3








37.8
24.9
37.8
24.9
45.6
30.1








15.5
10.2
' 15.5
10.2
18.7
12.3 '








21.6
14.3
21.6
14. T
91 .6
14.3








34 . 1
22.5
34.1
99 s
34.1
2?. 5








620
409
620
4fl9
690
409








642
424'
64?
4?4
A/,9
494








0
483
0
483
0
	 6.04. 	







K_04_
17 . 1
l 7 1
17.1
20 6
_20^6 	








-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1974
Region:     2
Data Type:  6-SI
Page 142  of  192
Hcgulntory
Sccnnr Lu
19

20

21









Control
Strategy
Mix
1
2
.1
2
1
•>








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (1) F CU fi m H (r\ I (D .T m K (L)
->







, The



^









-e were r













o second













rv impat













ts in 19













74.

















































































(JO

-------
                       FORM 6

           SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:     2
Data Type:  b-Sl
Page 143  of  192
Regulatory
Sccnnrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (U C a) D CM F. H.1 V (l.\ r. H\ \l (L) I (L) J (L) K (U
0
=0
0
0
I Nr>r An
)








0
0
0
0
[ill ralil p









0
0
0
0










4.5
3.0
25.6
16.9










1.9
1.3
10.5
6.9










12.1
8.0
23.3
15.4










28.5
18.8
55.7
36.7










254
168
482
318










359
237
692
457










0
659
0
652










16.6
16.6
27.1
27.1










Cxi

-------
                       FORM  6
            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     2
Data Type:  6-SI
Page 144  of  192
UeRulntory
Sccnnrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F CU G CM H fM T CM T n .\ K__£L) 	
0
0
0
0
0
0








0
0
0
0
0
0








0
0
0
0
0
0








53.6
35.4
53.6
35, U
67.7
44.7








22.0
14.5
• 22.0
14.5
27.8
18.3








29.9
19.7
29.9
197
29.9
19.7





*


71.1
46.9
71.1
46 ,Q
71.1
46.9








620
409
6?0
/,na
620
409








888
586
ftftft
586
888
586








0
1015
n
1015
0
_L2fi5 	







J3t6^3 	
16.9
36 q
•)6.9
45.0
._45.D 	







0|
-0

-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:   Pecroleum Refining
Year:       1974
Region:      3
Data Type:  6-SI .
Page 145 of  192
HcRulntory
Scenario
19

20

21









Control
Strategy
Mix
1
2
1
2
1
9








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (L) G (L) H (U T CU .1 fM if tt.N
•>
-


J


^ There





-








were no













Sftrnnrlai













y •Jmp/irr-













•=! In 197




















































•










































Gi

-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:   PeLroleum Refining
Year:        1930
Region:      3
Data Type:  6-SI
Page 146 of  192
Regulatory
Scenario
19

20

21







;

Control
Strategy
Mix
1
' 2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (U G (L) H fU T fM .T fU V fM
0
0
0
0
1 »L
> Noc i








0
0
0
0

prfTttnatn








0
0
0
0

*








1.9
1.3
11.0
7.3










0.8
0.5
A. 5
3.0










5.2
3. A
10.0
6.7










8.2
5.4
16.0
10.6










152
100
285
18ft










154
102
296
1Q5










0
?fi?
0
	 na_-_









7.1
11 .6
11 6










Gi

-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:   PeCroleum Refining
Year:       1985
Region:      3
DaCa Type:  6-SI
Page 147 of  192
ttcgulntory
Scennrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (L) G (L) H a) I a) .1 m K d\
0
0
0
0
n
0








0
0
0
0
0
0








0
0
0
0
n
0








25.6
16.9
25.6
16.9
V.^
21.3








10.5
6.9
10.5
6.9
13.2
8.7





•


14.3
9.4
14.3
9.4
14.3
9.4








22.6
14.9
22.6
14.9
22.6
14.9








410
271
410
271
410
271








42T
279
423
279
423
279








0
484
0
484
0
_^







17.6
17.6
17.6
21.5
-2LJ5 	







Oj

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      4
Data Type:  6-SI
Page 148  of 192
Hegulntory
Sccnnr l.o
19

20

21









Control
Strategy
Mix
1
2
1
?
1
?








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (U F U.) C. (1.) H d.\ T n.\ T (L\ K (Ul
^

> Thei


-/










e were n













p second;













rv impac













ts in 19













74.


















































































-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Regiorj:      4
Data Type:  6-SI
Page 149  of  192
IleRulntory
Scennrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (L) G (M H ^^ T ^T.^ J (U K (L)
29.1
19.2
40.0
26.6
N
Not Ap









19.2
12.7
26.4
17.6
plicable









9.6
6.3
13.2
8.7










0
0
0
0










0
0
0
0










0
0
14.fi
9.6










0
0
3R.8
?V6










0
0
?fiT
174










0
0
434
286










0
n sn
0
1142










IS.fL
lfi.fi
26.7
2.6.7

— _ — . —








-------
                      FORM 6

           SECONDARY IMPACT INDICATORS
Industry:
Year:
Region :      4
Data Type:  6-SI
Page 150 of  192
Petroleum Refining
1985
Regulatory
Scenario
19

20 •

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A fL) B CU C. (!.} D (L) E (L) F (U G fM H CM T m J (D _K 1D_
24.3
16.1
24.3
16.1
41.2
27.2








16.1
10.6
16.1
10.6
27.2
18.0








8.0
5.3
8.0
5.3
13.6
9.0








103
68
103
68
131
86.5








42.2
27.9
42.2
27.9
53.7
35.4








16.8
11.1
16.8
11.1
22.5
14.9








45.0
29.7
45.0
29.7
59.9
39.5








299
197
299
197
401
265








499
.329
499
329
668
441








0
1557
n
1557
1946








31 .0
31 .0
3] 0
31.0
43.1
43.1








Cr,

-------
                      FORM 6
           SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      5
Data Type:  6-SI
Page 151  of 192
UcRiilntory
Sceunrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
?








CONTROL EQUIPMENT
A (L) B (L) C (L) D a) E (L) F (L) G (L) H (L) I a) J (M
\

t Thei


J










e were p













T second;













—












l-s 1n 19













f



































































K_ax_













OJ

-------
                       FORM 6

            SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      5
Data Type:  6-SI
Page  152 of  192
Regulatory
Scenario
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D CU E CL) F H.1 r. (1.\ H (I,1* T (1.1 T (l.\ K (11
9.3
6.1
15.6
10.3
\ Nnf A
)








6.1
4.1
10.3
6.8
fxp-l±eabl








3.0
2.0
5.1
3.4










0
0
0
0










0
0
0
0










2.0
1.3
2.7
1.8










6.2
4.1
8.3
5.4










2.7
1.8
35.7
?3-6










59.4
39.2
80.2
57.9










0
311
0
307










5.4
5.4
8.4
fi 4










Go

-------
                      FORM 6

           SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     5
Data Type:  6~SI
Page 153  of  192
Uopulntory
Sconnrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A a) B a) c a> D ru E m F a.\ G a.) H (u i cu j ru K av
23.9
15.8
23.9
15.8
29.6
19. S








15.8
10.4
15.8
10.4
19.5
12.9








7.9
5.2
7.9
5.2
9.8
6.4








21.1
13.9
21.1
13.9
33.2
21.9








8.6
5.7
8.6
5.7
13.6
9.0-








5.5
3.6
5.1)
3.6
6.1
4.0








16.9
11.2
ifi 1
11.2
18.9
12.5








75.8
50.0
75 ft
50.0
84.7
55.9







	 ! 	
163
108
1^3
108
1R1
119








0
368
0
368
n
460








7-5
7.5
7 s
7.5
-KLJ 	
10r3








Ul

-------
                      FORM 6

           SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1974
Region:     6
Data Type:  6-SI
Page 154  of  192
Regulatory
Scennr lo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
?








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (L) G (1.) H CM I (U J OO K n,>
"N

Thei













e were p













T 5?err>nfl;













ry Impqr













rs in 10







•





7,

















































































03

-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      6
Data Type:  6-SI
Page 155  of 192
Ilcp.ulntory
Scenario
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (U F (L) G (L') H (U I (U J (I.) K (Li
0
0
4.3
2.8
-•k
Not A
-








0
0
2.8
1.9
plicablc









0
0
1.4
0.9










14 . 3
9.4
22.9
15.1










5.8
3.9
9.4
6.2










0
0
1.4
0.9










0
0
2.7
1.8










0
0
35.7
23.6










o
0
41.6
27.5










0
415
0
411










4 8
4.8
8.8
8.8










0)

-------
                        FORM 6

             SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      6
Delta Type:  6-SI
Page 156  of 192
llej»ulntory
Scenario
19

20

21









Control
Strategy
Mix
1
2
1
2
1 •
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (L) G a) H (1) I (L) J fU K fM
46.9
31.0
46.9
31.0
46.9
3.1.0








31.0
20.4
31.0
20.4
31.0
20.4








15.5
10.2
15.5
10.2
15.5
10.2








.51.5
34.0
51.5
34.0
67.4
44.5








21.1
13.9
21.1
13.9
27.6
18 _•)








4.4
2.9
4.4
2.9
5.9
\ Q








7.9
5.2
7.9
5.2
10.4
6 Q








116
77
116
77
161
106








131
86
131
86
175
116








0
538
0
538
n
673








11 .3
11.3
11.3
11 .3
15.5



	



u

-------
                       FORM  6

            SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:      7
Data Type:  6-SI
Page 157  of 192
llegulntory
Scenario
19

20

21









Control
Strategy
Hlx
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D rU E m F m r, n.\ H rT^ T n\ J (L) K (L)


, Ther













—












seronda













ry Impart













s in 197































































































Gj
\i
a-

-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:
Year:
Region:
Data Type:  6-SI
Page 158  of  192
Petroleum Refining
1980
7
Hcf»ulntory
Sccunrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C a) D (L) E (L) F (L) G (L) H (U I fU J (L) K (L)
133.5
88.1
122.6
80.9
I Not Ap
J








88.1
58.2
80.9
53.4
il irabl f









44.0
29.1
40.4
27.7










61.3
40.5
140.2
92.5










25.1
16.6
57.5
37.7










46.0
30.4
83.2
54.9










127.9
84.4
231.7
152,9










770
508
1391
91fl










1366
902
2471
1631










0
2777
n
2758










67 1
67.1
96-0
96.0





	



Oi

-------
                       FORM 6

            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      7
Data Type:  6-SI
Page 159  of  192
Rcgulntory
Sccunr I.o
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2 .








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (L) G (L) H (L) I (L) J a) K ' ai
88.8
58.6
88.8
58.6
99.5
65.7








58.6
38.7
58.6
1ft. 7
_&5_7__
43.4








29.3
19.3
29.3
19.3
32.8
21.7








322.8
213.0
322.8
213.0
411.6
271.7


.





132.3
87.3
132.3
ft? 1
16ft. ft
111. A







	 4 	
113.0
74.6
113.0
74.6
118T4
78.1








314 . 6
207.8
314.6
207.8
329,7
217.6








1891
1248
1891
1248
IQftl
1307








3356
2215
3356
2215
3516
2321








0
4416
ft
4416
0
5520








112.0
1.12.0
112,0
112.0
146.9
146.9








00

-------
                      FORM  6
           SECONDARY  IMPACT INDICATORS
Industry:   PeLroleum Refining
Year:       1974  .
Region:     8
Data Type:  6-SI
Page 160  of 192
UeRulntory
Sccnnrio
19

20

21









Control
Strategy
Mix
1
2
1
2
1.
?








CONTROL EQUIPMENT
A (L) B fL) C fU D (L) E (L) F (L) G (L) H (L) I (L) .1 fM K H.^


Ther













|2 were ni













seconda













ry impac




•o








s in 19 /













4.

















































































M

-------
                       FORM 6
            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      8
Data Type:  6-SI
Page 1.61  of 192
Regulatory
Scennrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (D B (D c rn n m E (U ' F (D c (L) H (U I a) J (U K ru
0
0
3.2
2.1
Not /









0
0
2.1
1.4
pplicabl









0
0
1.0
0.7










10.5
6.9
16.8
11.1




-



	 6—
4.3
2.8
6.9
/,.S










0
0
1.1
0.7










0
0
0.9
0.6










0
0
40.1
26. 5










0
0
32.7
?1 6










0
305
0
302










3.5
6.5
6.5










XJ

-------
                        FORM  6

             SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      8
Data Type:  6-SI
Page 162  of 192
Hcgulntory
Scenario
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L> D (U E (1.) V (L) G tL) H CM I (L) J (I.) K fLl
34.7
22.9
34.7
22.9
34.7
22.9








22.9
15.1 '
22.9
15.1
22.9
15.1








11.4
7.6
11.4
7.6
11.4
7.6








37.8
24.9
37.8
24.9
49.7
3?. ft








15.5
10.2
15.5
10.2
20.4
11.4








3.2
2.1
3.2
2.1
4.3
9. ft








3.1
2.0
3.1
2.0
4.4
2.9








112
74
112
74
147
97








95
63
95
63
128
84








0
397
0
3
-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:     9
Data Type:  6-SI
     163  of 192
Hcgulntory
Sccnnrio
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F a) G fU 11 m T tt.1 l fM K fU


> Ther













e were nc













seconds













rv impac













s in 19:













,


•















































































-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   PcCroleum Refining
Year:       1980
Region:     9
Data Type:  6-SI
Page 164  of 192
Uegulntory
Scennrlo
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (1.) F (l.\ G (L) H (L) I (U J (U K (L)
16.5
10.9
20.1
13.3
1 Not
J








10.9
7.2
13.3
8.8
Applicab









5.4
3.6
6.7
4.4
.e









0
0
0
0










0
0
0
0










3.7
2.4
0
0










13.3
8.8
. 0
0










31
21
0
0










110
73
0
0










0
1117
0
1117










19.4
19 . 4
26.6
26.6





	




-------
                       FORM 6
            SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1935
Region:      9
Data Type:  6-SI
     165  of 192
llogulntory
Sccnnr lu
19

20

21









Control
Strategy
Mix
1
2
1
2
1
2








CONTROL EQUIPMENT
A (L) B (L) C (L) D (L) E (L) F (L) G (L) H (L) 1 (L) .7 m K (1\
96.8
63.9
96.8
63.9
115.6
76.3








63.9
42.2
63.9
42.2
76.3
50.4








32.0
21.1
32.0
21.1
38.1
?5.?








66.1
43.6
66.1
43.6
120.4
79.5








27.1
17.9
27.1
17.9
49.3
32.6


%





21.2
14.0
21.2
14.0
26.0
17.2








77.1
50.9
77.1
50.9
94.0
	 62.0







175
116
175
116
219
145








630
416
630
416
77?
510








0
1792
0
1792
0
_224Q_







39.4
39.4
39.4
39.4
_iUi_
53.5

	





CO

-------
                                    FORM  6

                         SECONDARY  IMPACT INDICATORS
Industry;
Year:
Region:
Dana Type:
Petroleum Refining
1974
I
6-SI
                                                                      Page 166  of 192
llc|julatory
Sceimrtu
22




23




24




25




Control
Strategy
Mix
1
2
1
4
V
1
2
3
4
S
1
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A


















>
(W)









' The










B (W)









re were










C .(W)









10 reflnt










D (U)









rles in










E (W)





.



legion 1










F (W)









1n 1974.










C (W)



























































































	











CO

-------
                                   FORM  6
                        SECONDARY  IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1980
Region:     1
Data Type:  6-SI
Page ,16,7 of 192
Rc[>ulntory
Scennr lo
22




23




24




25




Control
Strategy
Mix
3
2
3
/
5
1
2
3
4
5
1
2
1
4
S
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
I

) Regi


0
0
0
0
0
0
0
n
0
n
0
0
0
0
0
B (W)


.atory s


0
0
n
0
0
0
0
n
n
n
0
0
0
0
0
C (W)


enario c


1
1
1
1
1
1
1
1
1
1
0
0
0
0
0
D (W)


oes not


3,5
3-5
•\ S
3.5
3.5
3.5
3.5
3 *
1 S
3.5
0
0
0
0
0
E (U)


satisfy .


0
0
n
0
0
0
n
0
n
0
l
1
1
1
1
F (U)


980 EPA


0
0
n
0
0
0
n
0
n
0
3.5
3.5
3.5
3.5
3.5
G (W)


requirem


0
0
n
0
0
0
n
0
n
0
1370
1370
1370
1370
1370



nts.
















































































P

-------
                                    FORM 6

                         SECONDARY IMPACT INDICATORS
Oi
CO
Oo
Industry:   Petroleum Refining
Year:       1935
Region:     i
Data Type:  6-SI
     168  of 192
llcftulntory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
1
/,
5
1
2
3
i
5
1
2
3
/,
i
]
2
3
A
' 5
CONTROL EQUIPMENT
A (W)
\

' Regul

s
"V

Regnl

/
N

/ Recul

J
0
0
0
0
0
B (W)


Jtory Sc




irnry Sr




itorv Sc


n
0
0 .
0
0
C (W)


narlo d<




• nfirl (\ f\f




marlo do


0
Q
0
0
0
D (W)


es not s









es not s


0
0
0
0
0 ,,
E (un


itisfy 1!




itisfy I1




itisfv 1'.


6
6
6
6
6
r cm


85 EHA i




a^-EEA-t



85 EPA >


13.5
]3.5
13.5
13.5
13.5
C (W)

equlreme




4<|4jic-ainyi



->qulreme


530Q
5300
5300
5300
5300



ts.









ts.







































































-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:.   Petroleum  Refining
Year:        1974
Region:      2
Data Type:  6-SI
Page 169  of 192
Ungulntory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
•i
1
2
1
4
1
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
5
5
S
	 i_
5
•v

Excei

/
~\

1 Rxrpr

J
-^

Excee

j
B m
10.5
10.5
in s
in. s
10.5


ds 1974




,!<; 1Q74




is 1974


C (W)
13
13
11
13
13


legulatoi




tpgnlal-ni




teRiilatoi


D (W)
24.4
24.4
?& &
?4.4
24.4


v reoulr




y rAqnlv




v requir


E (W)
0
0
n
n
n


iments.




^monl-c




:ments .


F rw)
0
0
n
n
0















G fW)
0
0
0
n
n




































































































-------
                                   FORM 6

                        SECONDARY IMPACT INDICATORS
Industry:   PeCroleum Refining
Year:       1980
Region:      2
Data Type:  6-SI
Page 170 of 192
nef>ulntory
Sccimrlo
22




23




24




25




Control
Strategy
Mix
1
2
1
4
5
1
2
3
4
S
1
2
3
. A
S
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
*X

1 Regu:

S
0
0
0
0
n
0
0
0
0
0
0
0
0
0
0
B (W)


atory sc


0
0
0
0
n
0
0
0
0
n
0
0
0
0
0
C (W)


:nario d<


21
21
21
21
?1
21
21
21
21
21
0
0
0
0
0
D (W)


es not £


36.8
16. ft
36.8
36.8
Ifi.H
23.4
23.4
23.4
23.4
23.4
0
0
0
0
0
E (W)


atisfy 1


0
0
0
0
n
0
0
0
0
0
21
21
21
21
21
F (W)


80 EPA i


0
0
0
0
n
0
0
0
0
0
23.4
23.4
23.4
23.4
23.4
G (W)


equireme


0
n
0
0
n
0
0
0
0
0
9300
9300
9300
9300
9300



its.
















































































Go

-------
                                    FORM 6
                         SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     2
Data Type:  6-SI
Page 171  of 192
Regulatory
Scennrlu
22




23




24




25




Control
Strategy
tllx
1
2
3
L
5
1
2
3
4
S
1
2
3
4
5
1
2
3
4
5
CONTROL KlJim'MENT
A (V)
^

/ Regul

s
1

I Regul

j
^

/ RCRU]

.
0
0
0
0
0
B (U)


atorv sc




•ifory sr




itorv sc


0
0
0
0
0
C (W)


nario d<




•.narlo t\i




nario dc


0
0
0
0
0
D (W)


os not a




es nor s




es not s


0
0
. 0
0
0
E (W)


tisfv 1!




irisfy 1<




itlsfv l^


25
25
25
25
25
V fW)


85 EPA t




flS EPA r




85 EPA r


27.3
27.3
27.3
27.3
27.3
C (W)


equlreroe




''
-------
                                    FORM 6
                         SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1974
Region:      3
Data Type:  6-SI
Page 172  of 192
llcgulntory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
S
1
2
3
4
5
1
?
3
u
5
1
2
3
4
5
CONTROL EQUIPMENT '
A (W)
3
3
3
3
N

/ Excei

)
•\

,' Excec

J
•^

f Excee

y
B (W)
1.8
1.8
1.8
1.8
1.8


ds 1974




els 1974




Is 1974


C (W)
7
7
- 7
7
7


•eeulatot




egulatoi




'egulatoi


D (W)
4.2
4.2
4.2
4.2
4.2


v requir




v requir




y requir


E (W)
0
0
0
0
0


jmenCs.




iments.




jinents.


F (W)
0
0
0
0
0


.












G (W)
0
0
0
0
0














































































	




















(Xi

-------
                                     FORM 6

                         SECONDARY  IMPACT INDICATORS
Indus try:
Year:
Region:      -•
DaLa Type:  6-SI
Page 173  of 192
Petroleum Refining
1980
3
 Go
CQ
00
Rcgulntory
Scennrlo
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
•)
1
4 •
S
1
2
3
4
5
CONTROL EQUIPMENT
A (W)


> Regu

)
0
0
0
0
0
0
0
0
0
n
0
0
0
0
0
B (W)


dtory sc


0
0
0
0
0
0
0
0
0
n
0
0
0
0
0
C (W)


Miario d>


14
14
14
14
14
14
14
14
14
M,
0
0
0
0
0
D (W)


es not s


11.6
11 fi
•11.6
11.6
11.6
9 1
9.1
q i
9.3
Q 3
0
0
0
0
0
E (W)


iclsfy 1


0
n
0
0
0
n
0
n
0
0
14
14
14
14
14
F (W)


80 EPA i


0
n
n
0
0
n
0
ri
0
0
9.3
9.3
9.3
9.3
9.3
G (W)


equlreme


0
n
n
0
0
n
0
n
0
0
3700
3700
3700
3700
3700



cs.

















































































-------
                                    FORM  6

                         SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:      3
Data Type:  6-SI
Page 174  of 192
Rcf>ulntory
Sccnnrlo
22




23 	



24




25




Control
Strategy
Mix
I
2
3
4
5
1
2
1
4
<;
1
2
3
4
5
1
2
3
A
5
CONTROL EQUIPMENT
A (W)
X

/ Recul

J


{Reeul


N

/ Regul

>
0
0
0
0
0
B (W)


jtory sc




itorv sc<




itory sc


0
0
0
0
0
C (W)


narlo dc




narlo do




nario do


0
0
0
0
0
D (W)


es not s




2S not s




es not s


0
0
0
0
0
E (W)


tlsfy 1<




itlsfv I1.




Ltisfv H


16
16
16
16
16
F (W)


85 EPA r




85 EPA r




85 UFA r


12,3
12.3
12.3
12.3
12.3
G.'(W)


iquiremei




iquiremei



iqni remei


4900
4900
4900
4900
4900



ts.




ts.




ts.

















































	




















Gi
OQ

-------
           FORM 6
SECONDARY IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:        191',
Region:     4
Data Type:  6-SI
Page 175 of 192
Ilnftiilutory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
•it
5
1
2
3
4
5
1
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
10
10
10
10
10
•^

( Fxrf»f

/
•v

i

/
•v

/ Excee

/
B (W)
16.5
16.5
16.5
16 .5
16.5


Is 1Q7A




Ic 1Q7/I




Is 1974


C (W)
22
22
22
22
22


•pj>ii1 n fnr









enulatot


D (W)
38.6
38.6
38.6
38.6
*
3fl f.


y rpfjiilr




ji T-pqiil r




y reaulr


E (W)
0
0
0
0
0


•mpnrs




inpnt" Q




ments .


F (W)
0
0
0
0
n















G (W)
0
0
0
0
n




































































































-------
                                    FORM 6

                         SECONDARY IMPACT INDICATORS
Industry:
Year:
Region :      *
Data Type:  6- SI
Page 176  of  192
Petroleum Refining
1980
llegulntory
Sccnnrlu
22




23




24




25




Control
Strategy
Mix
1
2
1
4
5
1
2
3
4
5
1
2
T
A
s
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
^\

) Regul

0
0
0
0
0
0
0
n
0
0
0
0
0
0
. 0
B (W)


atorv sc


0
0
0
0
0
0
0
0
0
0
0
0
•o
0
0
c (w)


mario di


32
32
32
32
32
32
32
1?
32
32
0
0
0
0
0
0 (W)


es not s


55.1
55.1
55.1
55.1
55.1
34.5
34, 5 _
V, 5
34.5
34.5
0
0
0
0
0
E (W)


idsfv 1<


0
0
0
0
0
0
0
0
0
0
32
32
32
32
32
F (W) •


80 RPA i


0
0
0
0
0
0
0
0
0
0
34.5
34.5
34.5
34.5
34.5
G (W)


^qu j rpHl^


0
0
0
0
0
0
0
n
0
0
13,700
13,700
13,700
1 3 , 700
13,700



fs .





























































	










	





Go
-0

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   1'ecrol.euni  Refining
Year:        1985
Region:      4
Data Type:  6-SI
Page 177  of 192
Hc|>iilntory
Sccnnrlu
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1
2
3
4
5
1
?
3
4 .
5
1
2
3
4
5
CONTROL EQUIPMENT
.A (wl_
\

f Regul

/
x

/ ReRul

/
^\

' Regul

J
0
0
0
0
0
n (w)'

atory sc




jtorv sc




itory sc


0
0
0
0
0
C (W)


:nario di




•nario dc




nario do


0
0
0
0
0
" (WL


es not u




es not s




2s not s


0
0
0
0
0
E (W)


tlsfy 1!




itlsfv 15




itisfy 1<


32
32
32
32
32
F (W) 1 G (W)


85 EPA r




85 EPA r




85 EPA r


36.1
36 . 1
36.1
36.1
36.1


tjqutreme




2quiremci




iquiremc


1 4 , 300
14,300
14,300
14,300
14,300



ts.




ts.




CS.







































































-------
                                     FORM  6

                          SECONDARY IMPACT INDICATORS
Industry:    I'eLrolcuin Re Ci.
Year:        1974
Region:      5
Data Type:   6-SI
Page  178 ol: 192
ItcRiilntory
Sconnrlo
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1
?
3
4
5
1
2
3
A
5
1
2
. 3
4
5

A (W)
4
4
4
4
-X



J
-\



/
•>



/


1 Excee




/ Kxcee




lixcee


p (w)
3.7
3.7
3.7
•\. 7
3.7


Is 1974 1




Is 1974




Is 1974


C (W)
9
9
9
9
' 9


egulatoi




epulator




egulator


CONTROL EQUIPMENT
D (W)
8.6
8,6
8.6
8.6
8.6


y requir




v requir




y requir


E (W)
0
0
0
0
0


Mnencs .




:ments.




mencs .


F (W)
0
0
0
n
0















c: (w)
0
0
0
0
0



























































— 	






































u
4)

-------
                                   FORM 6
                        SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1980
Region:      5
Data Type:  6-SI
Page 179  of 192
Ilcp.ulnlory
Sccnnrlu
22




23




24




25




Control
StruLcp.y
Mix
1
2
3
4
5
1
2
3
4
5
L
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
•N

/ Regul

S
0
0
0
0
0
0
ft
0
0
0
0
0
0
0
0
B (W)


itory sc


0
0
n
0
0
ft
0
0
0
0
0
0
0
0
C (W)


nario 
-------
                                    FORM 6

                         SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1985
Region:     5
Data Type:  6-SI
Page 180  of 192
Hcftiilnl oi y
Scennrlo
22




23




24




25




Control
Strategy
Mix
1
1
3
U
5
1
?
3
4
S
1
2
1
4
5
1
2
3
4
5

A (W)
-•>



/
•^



}
-\



s


[ Reg,,]




I
[ Rppnl




\
R/M.1,1


0
0
0
0
0
B (W)


ntpfv sc









i r n r v s c '


0
0
0
0
0
c (w)


:nario dr




n^ri" d-1




nar'o c'°


0
0
0
0
0
C(
D (W)


es not s









•« nor q;


0
0
0
0
0
JNTROI. EQUIPMEMT '
-£ (M

itiafy 1<




iti&£y— li




Msfy TJ


17
17
17
17
17 .
_lL_CklX_

fiS F;PA r




aS-EEA-c



RS KPA r


1?.0
J2.9
12.9
1? <)
12.9
r, 
-------
           FORM 6

SECONDARY IMPACT INDICATORS
Indus cry:   Petroleum  RofinIng
Year:       1971
Region:     6
Data Type:  6-SI
Page 181  of 192
Hc:j»ul ntory
Sccnnrlu
22




23




2k




25




Control
St mingy
Mix
1
2
3
4
S
1
2
3
1
•i
1
2
3
4
5
1
2
3
4
5
CONTROL KQUIl'MEHT
A (W)
5
5
5
	 L_
s
X

) Excee

/
*v

Excet

/
-v

Excee

/
B (W)
6.0
6.0
6.0
6.0
6 n


ds 1974




els 1,974




Is 1974


C (W)
13
13
13
13
1 3


legulatoi




(egulatoi1




tegulatoi


1) (W)
14.0
14.0
14.0
14.0
i/, n


y requir




V retiuir




y requir


E (W)
0
0
0
n


;ments.




;ments.




:mencs .


0
0
0
0
n















« (w)
0
0
0
0
n


v

































































































-------
                                    FORM 6

                         SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1930
Region:      6
Data Type:  6-SI
Page 182 of 192
llegulntory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4 '
5
1
2
3
4
5
1
2
3
4
•;
1
2
3
4
5
«
CONTROL EQUIPMENT
A (W)


/ Regul

)
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
B (W)


itorv sc


0
0
0
0
0
0
0
0
n
0
0
0
0
0
0
C (»)


u^

18
18
1ft
18
18
18
18
18
18
18
0
0
0
0
0
1) (W)


es not s


20.0
20.0
?0.0
20.0
20.0
12.3
12.3
12.3
12.3
12.3
0
0
0
0
0
E (U)


itisfv r


0
0
0
0
0
0
0
0
0
0
18
18
18
18
18
F (Wl_

80 EPA r


0
0
0
0
0
0
0
0
0
0
12.3
12.3
12.3
12.3
12.3
G (v)


cqulreme

0
0
0
0
0
0
0
0
0
4900
4900
4900
4900
4900



cs.









































































	





Co

-------
                                    FORM 6

                         SECONDARY IMPACT INDICATORS
Go
4^
Co
Industry:   Petroleum Refining
Year:       1985
Region:      6
Data Type:  6-SI
Page 183 of  192
ItcRiilntory
Sccnnrlo
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1
?
3
4
5
1
2
T
4
S
1
2
3
4
5
.CONTROL EQUH'MENT
A (W)
\

1 Regul

/*


' Kegul

)
-\

/ Rfj.nl

/
0
0
0
0
0
B (W)


atory sc<




itory sec




irnry ctr*


0
0
0
0
0
c (w)


narlo do




nario do




n.^rin i\f\


0
0
0
0
0
n (w)


js not s




:s not s;




^>: nnl- «:


0
0
0
0
0
E (W)


tisfy 1<




tlsfy iy




ri^fy 10


18
18
18
18
18
F (W)


85 EPA r




85 El1 A r




RS PPA r


12.3
12.3
12.3
12.3
12.3
G (W)


quiremei




:qulremci




• q^p yom/ni

4yoo
4900
4900
4900
4900



cs.




ts.




t °


































'
	 ~
























	








-------
                                   FORM  6

                        SECONDARY  IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1974
Region:     7
Data Type:  6-SI
Page 184  of 192
Regulatory
Scenario
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
1
2
1
4
5
1
2
3
• 4
5
1
2
3
.4
5
CONTROL E(}U11'MEHT
A (U)
22
22
22
22
22
\

/ Rxrfi

/
\

/ Excec

J
*\

> Exce

/
B CW)
43.2
43.2
43.2
43.2
43.2


As. 1074




ds J974




ds 1974


C fW^
52
52
52
52
52


R|»J>!|1 AlTl




Regulate




Jegulato


D (W)
101.8
101.8
101.8
101.8
101-8


•y rpqiii i




•v requii




:y requii

,
E fW)
0
0
0
0
0


i^|T)f>nr ^




(?mp n r s .




ements.


F rw)
0
0
0
0
0















C, (V)
0
0
0
0
0



































































































Ui

-------
                                    FORM 6
                        SECONDARY  IMPACT INDICATORS
Industry:   Petroleum  Refining
Year:       1980
Region:      7
Data Type:.  6-SI
Page 185 of 192
HcRulntory
Sccnnrto
22




23




24




25




Control
Strategy
Mix
1
2
1
/i
5
1
2
•\
it
5
1
2
1
i
5
1
2
3
4
5
CONTROL EQUIPMENT
A (v)
*v

-V Hega

,/
0
0
fl
0
0
0
0
0
n
n
0
0
0
0
0
B (U)





0
0
n
0
0
0
0
0
n
0
0
0
0
0
0
C (W}





81
8]
fll
81
81
81
81
81
/
fll
81
0
0
0
0
0
D (vO


ea not s


162.6
162.6
1ft?. ft
162.6
162.6
106.7
106.7
106. 7
inA 7
106.7
0
0
0
0
0
E (W)


atisfv 1


0
0
0
0
0
0
0
0
n
0
81
81
81
81
81
F (W)


80 EPA i


0
0
0
0
0
0
0
0
0
0
106.7
106.7
106.7
106.7
106.7
C (W)


equireme


0
0
0
0
0
0
0
0
n
0
42.300
42,300
42,300
42.300
42,300



its .













































	

































o

-------
           FORM 6

SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       1935
Region:     7
Data Type:  6-SI
Page 186  of 192
Kef>uin tory
Scctinr to
22




23




24




25




Control
Strategy
Mix
1
2
1
4
5
1
?
3
4
5
]
2
3
4
5
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
\

Rpgul


N

1 Regu]

J
•v

' Regul

S
0
0
0
0
0
B (W)


irr>iry *ir




atory sc




jtory sc


0
0
0
0
0
C (W)


•nnrln At




marlo dc




:narlo dc


0
0
0
0
0
D (W)


p<* nnf »?




es not s




es not s


0
0
0
0
0
E (W)


irisfy T




itisfy 1!




itlsfy 1^


86
86
86
86
86
F (W)


ftS KPA r




85 EPA i




85 EPA r


1.28.0
128.0
128.0
128.0
128.0
P (W)

•
pqiil rpn)p




>quiretne




itjulreme


50,700
50,700
50,700
50,700
50,700



t-s.




ts.




ts.







































































-------
                                   FORM 6

                        SECONDARY IMPACT INDICATORS
Industry:   Petroleum Refining
Year:       197 A
Region:     8
Data Type:  6-SI
Page 187  of 192
Kcftulntory
Sccnnrlo
22




23




24




25




Control
Strategy
Mix
.1
2
3
4
5
1
?
3
4
5
1
2
3
U
5
1
2
3
4
5
CONTROL EQUIPMENT
A (U)
10
10
10
10
10
\

} Excet

/


/ Excet

>
^

1 Excee

/
B (U)
4.0
4.0
4.0
4.0
4.0


ds 1974




Is 1974




Is 1974


C fwl
23
23
23
23
23


legulatoi




egulatoi




egulucoi


D fW^
9.4
9.4
9.4
9.4
9.4


y requlr




v requir




y rec|ulr


-li-CW
0
0
0
0
0


:ments .




•ment s .

-


intents.


_£_XUX_
0
0
0
0
^-




,









-i^ux_
0
n
0
0
0














































































	




















§

-------
                                      FORM 6

                          SECONDARY  IMPACT INDICATORS
Indus ti-y:    I'ecroleum Refininj?,
Year:        1'JSO
Region:      8
DiiLa Type:   6-SI
I'at-o 188   of 192
Ungulntory
Scenario
22




23




24




25




Control
Strntc|>y
Mix
1
2
"1
A
S
1
2
3
/,
5
1
2
•)
L
5
1
2
3
4
5
CONTUOI. KQUU'NENT
A (W)
*\

/ Rfpul

)
0
0
0
n
0
0
0
n
n
o
0
0
0
0
0
B (W)





0
0
0
n
0
0
0
n
0
o
0
0
0
0
0
c (w)





33
33
•n
11
33
33
33
IT
33
11
0
0
0
0
0
D (W)





13.4
13. A
13-4
1 1 i
13. A
8.3
8.3
R. 1
8.3
ft 3
0
0
0
n
0
E (W)


iLlsfy 1'

0
0
0
n
0
0
0
n
0
n
33
33
33
33
33 •
F (W)


80 El'A i


0
0
0
n
0
0
u
(i
0
0
8.3
8.3
8.3
8.3
8.3
c: (w)


t*qn i rt'mc-

0
0
0
ft
0
0
f)
ft
0
0
3300
3300
3300
3 '100
3300



f s .
















































































(I)

-------
                                   FORM 6

                       SECONDARY  IMPACT INDICATORS
Industry:    Petroleum Refining
Year:       1985
Region:     8
Data Type:  6-SI
Page 189 of 192
Heroin tory
Scciinrlo
22




23




24




25




Control
Strategy
Mix
1
?
3
4
5
1
2
3
4
•5
1
2
3
4
5
1
2
3
4
5
CONTROL, ECJUIl'MENT
A (W)
"V

' Refiu;

S
~\

t Regul

/
-x

/ ReRu]

/
0
0
0
0
0
B (V)


atory sc




itorv sc




atory sc


0
0
0
0
0
C (W)


inarlo di




:narlo di




;nario di


0
0
0
0
0
D (W)


es not s




es not s




es not s


0
0
0
0
0
E (W)


dtlsfy 1




itlsfy 1'




ittsfy ]>


33
33
33
33
33
F (W)


85 EPA i




85 EPA i




85 EPA r


8.3
8.3
8.3
8.3
8.3
0 (V)


equireme




oquireme




L'qul rente


3300
3300
3300
3300
3300



ts.




ifs .




its.






































































O

-------
                                    FORM 6

                         SECONDARY IMPACT INDICATORS
Industry:   Pecroleum Refining
Year:       1974
Region:      9
Data Type:  6-SI
Page 190  of 192
HeRulntory
Scenario
22




23




24




25




Control
Strategy
tllx
1
2
3
it
s
1
2
3
4
s
1
2
3
4
s
1
2
3
4
5
CONTROL EQUIPMENT
A (W)
14
14
14
i/.
^




N



S
^.



-


1 Excet




1 Excet




1 Excee


B (WV
16.7
16.7
16.7
16.7
16.7


ds 1974




ds 1974




Is 1974


C (W)
•v,
34
'14
34


teculatoi




tegulator




:ejjulatoi


D (W)
Ifl 3
38.3
38.3
38.3
38.3


V requir




y requlr




y requlr


E (W)
0
0
0
0


iments.




:ments.




: incuts.


F (W)
0
0
0
0
0















C fW)
0
0
0
n
0



































































































-Q
  '

-------
           FORM  6

SECONDARY IMPACT INDICATORS
Industry:    Petroleum Ucfi.niny
Year:        1980
Rej-ion:      9
Data Type:   6-SI
Page 191 of  192
Unp, ul n Lory
Scennrlo
22




23




24




25




Control
Strategy
Mix
1
2
3
4
5
]
2
3
4
5
1
2
3
4
5
1
2
3
4
5
CONTROL KQUIl'MENT
A (W)
-\

} Regu

J
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
B (W)


atory sc


0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
C (W)


jnarlo di


54
54
54
54
54
54
54
54
54
54
0
0
0
0
0
D (W)


es not s


65.7
65.7
	 	 65.7
65.7
65.7
44.3
44.3
44 . 3
44,3
44 . 3
0
0
0
0
0
E (W)


itisfy 1


0
0
0
0
0
0
0
0
0
54
54
54
54
54
1' (W)


80 KPA i


0
0
0
0
0
0
0
0
0
0
44.3
44.3
44.3
44.3
44.3
(• (W)


equlreme


0
0
0
0
0
0
0
0
0
0
17,600
17,600
17,600
17,600
17,600



ts.

















































































-------
                                     FORM 6

                          SECONDARY IMPACT INDICATORS
Industry:   Pecroleum  Refining
Year:       1985
Region:     9
Diita Type:  6-SI
Page 192  of  192
llcgulnloi y
Scenario
22




23




2k




25




Control
Strategy
Mix
1
7
3
4
5
1
2
3
4
5
1.
?
3
4
5
1
2
3
ft
5
CONTROL EQUIPMENT
A (W)
V

' Regu!

/
•\^

1 Reeul

/
^

) ReKu]

/
0
0
0
0
0
B (W)


atory sc




atorv sc




;itory sc


0
0
0
0
0
C (W)


inario d<




^nario dt




;nario d(


0
0
0
0
0
D (W)


es not s




es nor. .s




es not s
•

0
0
0
0
0
E (W)


itisfy 1'




!Clsfv 1'




itisfy 1'


62
62
62
62
62
F (W)


85 EPA r




85 KPA r




85 EPA i


56
56
56
56
56
C (W)


cqulreme




equireme




QQiiiremt


22,200
22,200
22,200
22,200
22,200



its.




its.




its.






































































-C
0

-------
            APPENDIX C
United States Refineries By Company

-------
                               TABLE C-l — COMPLETE LIST OF  UNITED STATES REFINERIES BY COMPANIES
o
I
            COMPANY
1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
19.
20.
21.
22.
23.
24.
25.
26.
27.
28.
29
30.
31.
32.
33.
34.
35.
36.
37.
38.
39.
40.
41.
42.
43.
44.
45. I
Adobe Refining Co.
Allied Materials Corp
Amerada-Hess

American Petrofina


Amoco Oil









APCO Oil Corp.

Arizona Fuels Corp.

Ashland Petroleum




Atlantic Richfield Co.





Atlas Processing
Bay Refining - Dow Chem.
Bayou State Oil Corp.
Beacon Oil Co.
Berry Petroleum Co.
Big West Oil Co.
B. P. Oil Corp.
Bradford Petroleum
British Petroleum Co.
Calumet Refining Co.
Canal Refining Co.
Caribou Four Corners, Inc
mm mm
PRODUCTION CAPACITY


LOCATION
LaBlanca, Tex.
Stroud, Okla.
Fort Reading, N.J.
Purvis, Miss.
Eldorado, Kan.
Mt. Pleasant. Tex.
Port Arthur, Tex.
Savannah, Ga.
Wood River. 111.
Whiting, Ind.
Baltimore, Md.
Sugar Creek, Mo.
Handan, H. Dakota
Texas City, Tex.
Salt Lake City, Utah
Yorktown, Va.
Casper, Wyoming
Arkansas City, Kan.
Cyril, Okla.
Fredonia, Ariz.
Roosevelt, Utah
Calettsburg, Ky.
Louisville, Ky.
Tonawanda, N.Y.
Canton, Ohio
Findlay, Ohio (Seasonally)
North Slope, Alaska
Carson, Calif.
East Chicago, Ind.
Philadephia, Penn.
Houston, Tex.
Ferndale, Wash.
Shreveport, La.
Bay City, Mich.
Hosston, La.
Hanford, Ca.
Stephens, Ark.
Kevin, Hon.
Marcus Hook, Penn.
Bradford, Penn.
North Slope, Alaska
Princeton,' La.
Church Point, La.
Kirtland, N. Mex.
| IflBCrodBBah ••§
li\
REFINERY1 U
CAPACITY
(mVday)
676
875
11100
4530
3900
4130
13400
1910
17000
50100
1590
16700
7630
52900
6200
8430
6840
3980
1910
1590
1750
21000
3980
10300
9540
1590
763
26200
20000
29400
33900
15300
4610
2700
557
1910
477
815
15600
1110
200
382
398
350
••668 ••§

LUBES*1)
(mVday)
... _
143
—
—
—
—
—
—
—
1380
—
—
—
—
—
—
204
—
—
.-.-
—
—
—
—
—
_--
—
—
—
—
1030
—
—
—
200
—
—
—
—
493
—
270
—
—
•••-- ••

ASPHALT*1 ^
(m'/day)

192
—
—
318
1270
—
1270
1720
4930
1270
1030
—
843
398
—
246
223
207
—
—
1590
557
1590
1590
954
—
—
1650
3100
—
—
—
—
80
— .
160
52
—
—
—
76
—
—
••

COKE*1*
(metric tpd)
	
—
—
291
—
—
—
—
—
663
—
' 409
—
726
- — •
'645
...
—
—
—
—
—
—
—
—
...
—
1630
—
—
1180
1360
—
—
—
—
—
—
—
—
—
—
—
—


OPERATING* '
GASOLINE
OUTPUT
(mVday)

—
5090
2850
1690
1510
4170
—
5470
20000
—
5950
3180
39400
2770
3820
1570
2540
763
—
—
8080
1370
3500
4370
---
—
13700
7600
12600
20100
9740
1270
525
—
411
—
216
7710
286
—
—
200
—


-------
                             TABLE C-l  — COMPLETE LIST OF  UNITED STATES  REFINERIES  BY COMPANIES  (Continued)
O
 i
OJ
 46.
 47.
 48.
 49.
 50.
 51.
 52.
 53.
 54.
 55.
 56.
.57.
 53.
 59.
 60.
 61.
 62.
 63.
 64.
 65.
 66.
 67.
 68.
 69.
 70.
 71.
 72.
 73.
 74.
 75.
 76.
 77.
 78.
 79.
 80.
 81.
 82.
 83.
 84.
 85.
 86.
 87.
 83.
 89.
 90.
PRODUCTION .CAPACITY


COMPANY
Cenex
Champlin Petroleum Co.


Charter International Oil Co.
Chevron Asphalt Co.
Chevron Oil Co.


Cities Service Oil Co.
Clark Oil & Refining Corp.

Coastal States Petrochemical Co
Continental Oil Co.




Cosden Oil & Chemical Co.
Cotton Valley Solvents Co.
CRA Inc.


Cross Oil & Refining Co.
Crown Central Petroleum Corp.
Crystal Refining Co.
Delta Refining Co.
Derby Refining Co.
Diamond Shamrock Oil & Gas Co.
Douglas Oil Co. of Calif.

Eddy Refining Co.
Edgington Oil Co.
Edgington Oxnard Refinery
Evangel ine Refining Co1., Inc.
Exxon Oil Co.




Famariss Oil Corp.
Fletcher Oil & Refining Co.
Flint Chem. Co.
Gary Western Co.
Getty Oil Co.. Inc.


LOCATION
Laurel, Mon.
Corpus Christi , Tex.
Wilmington, Calif.
Enid, Okla.
Houston, Texas
Baltimore Md.
Perth Amboy, N.J.
El Paso, Tex.
Salt Lake City, Utah
Lake Charles, La.
Blue Island, 111.
Hartford, 111.
Corpus Christi , Tex.
Billings, Mon.
Commerce City, Colo.
Ponca City, Okla.
Westlake, La.
Hrenshall, Minn.
Big Spring, Tex.
Cotton Valley, La.
Coffeyville, Kan.
Pliill ipsburg, Kan.
Scottsbluff, Neb.
Smackover, Ark.
Houston, Texas
Carson City, Mich.
Memphis, Tenn.
Wichita, Kan.'
Sunray, Texas
Paramount, Calif.
Santa Monica, Calif.
Houston, Texas
Long Beach, Calif.
Oxnard, Calif.
Jenings, La.
Benica, Calif.
Bay town, Tex.
Baton Rouge, La.
Billings, Mon.
Lindon, N.J.
Monument, N. Mex.
Carson, Calif.
San Antonio, Tex.
Grand Junction, Colo.
Delav/are City, Del .

REFINERY(1)
CAPACITY
(m3/day)
6680
9860
4610
7870
11100
2150
14000
11300
7160
42600
10800
5720
21500
8350
4770
18600
13200
3740
10300
1230
5570
3180
795
771
15900
986
4610
4110
7470
5570
1300
517
4610
398
684
1 3800
63600
70800
7160
43700
795
2510
191
1320
22300

LUBES*1^ '
(m3/day)

—
—
175
—
—
—
—
—
1110
—
—
—

—
366
—
—
—
—
239
—
—
207
—
—
—
—
—
—
—
—
—
—
—
—
3980
2390
—
—
—
—
—
—
— .

ASPHALT^
(raVday)

—
—
223
636
1750
' 3980
795
	
	
716
—
80
557
525
477
—
—
1270
—
—
318
—
223
	
—
477
—
398
2230
922
—
1190
—
—
—
1910
4600
2070
7310
—
—
—
—
—

COKE*1*
(metric tpd)

—
522
150
—
—
—
—
	
908
—
409
454
—
—
454''
454
—
—
—
272
—
—
—
272
—
—
145
—
—
—
—
—
—
—
817
—
1960
227
—
—
—
—
363
1630

OPERATING^'
GASOLINE
OUTPUT
(mVday)
3070
5100
398
5380
4450
—
3420
5450
2850
17300
7600
6480
7080
3380
1700
9410
5600
1060
8740
—
2860
1510
350
—
8045
—
2230
2020
4130
986
—
—
—
—
95
12000
26500
33000
3700
18400
95
557
—
—
11700

-------
TABLE C-l — COMPLETE LIST OF UNITED STATES REFINERIES BY COMPANIES  (Concinued)
PRODUCTION CAPACITY



91.
92.
93.
94.
95.
96.
97.
98.
99.
100.
101.
102.
103.
104.
105.
106.
o 107'
, 108.
4> 109.
110.
111.
112.
113.
114.
115.
116.
117.
118.
119.
120.
121.
122.

123.
124.
125.
126.
127.
128.
129.
130.
131.
132.
133.
134.
135.


COMPANY
Gladieux Refinery
Golden Bear, Div.
Golden Eagle Refining
Good Hope Refineries
Gulf Oil 'Co.






Hawaiian Indep. Ref.
Howell Hydrocarbons
Hunt Oil
Husky Oil


Ind. Farm Bur. Coop.
Jet Fuel Refinery
Kern County Refining Co.
Kerr McGee Corp.

Koch Refining Co.
LaGloria Oil & Gas Co.
LaJet Inc.
Lakeside Refining Co.
Laketon Asphalt Refining, Inc.
Lion Oil Co.
Little America Refining Co.
Longview Refining Co.
Lunday-Thagard Oil Co.
MacHillan Ring - Free Oil Co,
Inc.

Marathon Oil Co.


Marion Corp.
Mid America Refinery Co., Inc.
Midland Cooperatives, Inc.
Mobil Oil Corp.







LOCATION
Fort Wayne, Inc.
Oildale, Calif.
Carson, Calif.
Good Hope, La.
Sante Fe Springs, Calif.
Belle Chasse, La.
Venice, La.
Cleves, Ohio
Toledo, Ohio
Philadelphia, Penn.
Port Arthur, Tex.
Barber's Point, Hawaii
San Antonio, Texas
Tuscaloosa, Ala.
North Salt Lake, Utah
Cheyenne, Wy.
Cody, Wy.
Mt. Vernon, Ind.
Mosby, Hon.
Bakersfield, Calif.
Cotton Valley, La.
Wynnewood, Okla.
Pine Bend, Minn.
Tyler, Texas
St. James, La.
Kalamazoo, Mich.
Laketon, Ind.
El Dorado, Ark.
Casper, Wy.
Longview, Tex. •
South Gate, Calif.

Norphlet, Ark.
Signal Hill, Calif.
Robinson, 111.
Detroit, Mich.
Texas City, Texas
Mobile, Ala.
Chanute, Kan.
Cushing, Okla.
Ferndale, Wash.
Beaumont, Texas
Buffalo, N.Y.
Paulsboro, N.J.
Augusta, Kan.
Torrance, Calif.
REFINERY*1'
CAPACITY
(m3/day)
1590
1670
2070
4680
8190
28700
4560
6690
8000
26800
49600
4770
493
2390
1830
3750
1700
2390
159
2050
1190
5090
17000
4450
1750
954
1350
7000
3500
1050
795

716
1510
31000
9220
9700
2390
493
3020
11400
51700
6770
15600
7950
19600
f 1 \
LUBES1"
(mVday)
- ••-
636
—
—
—
-j-
—
—
—
—
2010
—
—
—
—
—
—
—
—
—
—
—
—
—
__i
—
—
127
—
—
—

—
—
—
—
—
—
—
—
—
1400
—
1020
—
—
{ 1 \
ASPHALT1"
(mVday)

509
—
—
636
—
—
461
318
—
—
—
—
827
—
477
636
.-_
—
—
—
557
3180
—
—
—
413
954
318
—
254

199
—
—
1380
—
—
—
—
—
16
1190
—
1270
---
/ 1 \
COKE1"
(metric tpd)

—
—
—
—
763
—
—
—
—
1260
—
—
—
—
—
—
—
—
—
—
—
1180
73
—
—
—
—
—
—
—

—
—
817
—
—
—
—
73
—
1090
—
885
—
2540
OPERATING*2'
GASOLINE
OUTPUT
(mVday)
40
—
—
557
4530
16900
3550
3820
3790
15300
26500
—
159
191
652
2040
763
986
—
509
553
3930
6730
2730
—
191
—
2660
1700
239
—

—
—
11100
4640
3130
—
—
1540
4320
25600
3200
5660
3690
14100

-------
TABLE C-l — COMPLETE LIST OF UNITED STATES REFINERIES BY COMPANIES (Continued)
PRODUCTION CAPACITY



136.
137.
138.
139.
140.
141.
142.
143.
144.
145.
146.
147.
148.
149.
150.
151.
152.
153.
9 154.
u, 155.
156.
157.
158.
159.
160.
161.
162.
163.
164.
165.
166.
167.
163.
169.
170.
171.
172.
173.
174.
175.
176.
177.
178.
179.
180.
181.
182.


COMPANY
Mobile Oil Corp. , Inc.

Mohawk Petroleum Corp., Inc.
Mountaineer Refining Co., Inc.
Murphy Oil Corp.

National Cooperative Ref. Assoc
Navajo Refining Co.
Newhall Refining Co., Inc.
North American Petroleum Corp
Northwestern Refining Co.
OKC Refining Inc.
Osceola Refining Co.
Pasco, Inc.
Pennzoil Co.

Phillips Petroleum Co.





Plateau, Inc.
Powerline Oil Co.
Pride Refining Inc.
Quaker State Oil Ref. Corp.



Quintana-Howell
Rock Island Refining Corp.
Sage Creek Refining
San Joaquin Refining
Sequoia Refining Corp.
Seminole Asphalt Ref.
Shell Oil Co.







Skelly Oil Co.
Soirerset Refinery
Sound Refining Inc.
Southland Oil Co.


LOCATION
Joliet, 111.
East Chicago, Ind.
Bakorsfield, Calif.
LaBarge, Wy.
Meraux, La.
Superior, Wise.
McPherson, Kan.
Artesia, N. Mex.
Newhall, Calif.
Shallow Water, Kan.
St. Paul Park, Minn.
Okmulgee, Okla.
West Branch, Mich.
Sinclair, Wy.
Rouseville, Penn.
Falling Rock, W. Va.
Borger, Tex.
Kansas City, Kan.
Great Falls, Mon.
Woods Cross, Utah
Sweeney, Texas
Avon, Calif.
Bloomfield, N.Mex.
Santa Fe Springs, Calif.
Abilene, Tex.
Emlenton, Penn.
Farmers Valley, Penn.
Newell, W. Va.
St. Mary's, W. Va.
Corpus Christi , Tex.
Indianapolis, Ind.
Cowley, Wy.
Oildale, Calif.
Hercules, Calif.
St. Marks, Fla.
Martinez, Calif.
Wilmington, Calif.
Hood River, 111 .
Norco, La.
Ciniza, N.Mex.
Deer Park, Tex.
Odessa, Tex.
Anacortes, Wash.
El Dorado, Kan.
Somerset, Ky.
Tacoma, Wash.
Crupp, Miss.
REFINERY*1 }
CAPACITY
(mVday)
27800
7470
3510
80
14700
5880
8610
3330
1190
795
9540
3420
1510
6360
1590
795
15100
13500
906
3660
13500
17500
811
4530
2240
528
1030
1540
771
1590
4690
159
2700
4290
795
15900
15300
41300
38200
3180
45800
5090
14500
11700
445
716
668
/ 1 \
LUBES* "
(m3/day)
...
—
—
—
—
—
—
—
—
—
—
—
—
—
561
207
—
398
—
—
—
266
—
—
—
270
398
572
270
—
—
—
—
—
—
716
—
890
—
—
954
—
—
—
— •
302
—
f 1 \
ASPHALT1 ' '
(mVday)

—
—
—
—
1910
—
223
477
—
3500
223
—
366
—
—
—
477
127
350
—
—
—
795
—
—
—
—
—
—
477
—
534
—
398
1650
—
3580
954
134
604
—
—

—
413
229
n \
COKE1"
(metric tpd)
1540
—
—
—
—
—
318
—
—
—
-•-.
—
	
—
—
—
—
—
—
—
—
1090
—
—
—
—
—
—
—
—
—
—
—
—
—
—
1630
—
817
—
—
—
—
454
—
—
—

OPERATING* *
GASOLINE
OUTPUT
(mVday)
14500
3670
350
—
3590
2240
3350
914
—
—
3330
1990
—
2630
448
318
10600
6121
262
1750
9060
1 3600
350
2130
—
169
366
398
183
—
2500 '
—
—
2660
—
7880
7360
24800
20200
1830
19100
2420
7710
6150
—
—
—

-------
TABLE C-l — COMPLETE LIST OF UNITED STATES REFINERIES BY COMPANIES (Continued)
PRODUCTION CAPACITY



183.
184.
185.
186.
187.
188.
189.
190.
191.
192.
193.
194.
195.
196.
197.
198.
199.
0 200.
i 201.
°^ 202.
203.
204.
205.
206.
207.
208.
209.
210.
211.
212.
213.
214.
215.
216.
217.
218.
219.
220.
221.
222.
223.
224.
225.
226.
227.
228.
229.


COMPANY
Southland Oil Co.

Southwestern Oil & Ref. Co.
Southwestern Ref. Co.
Standard Oil of Calif.





•" "
Standard Oil of Ky.
Standard Oil of Ohio

Sun Oil Co.



Sunland Ref. Co.
Suntide Refining
Tenneco Oi 1 Co.

Tesoro-Alaskan Petr.
Tesoro Petroleum


Texaco, Inc.











Texas Asphalt & Ref. Co.
Texas City Refining
The Refinery Corp.
Three Rivers Refinery
Thriftv/ay Co.
Tonkawa Refining
Toscopetro Corp.
Total Leonard, Inc.
U.S. Oil J Refining


LOCATION
Lumberton, Miss.
Sandersvil le, Miss.
Corpus Christi , Tex.
La Barge, Wy.
Kenai , Alaska
Bakersfield, Calif.
El Segundo, Calif.
Richmond, Calif.
Barber's Point, Hawaii
Portland, Oregon
Richmond Beach, Wash.
Pascagoula, Miss.
Lima, Ohio
Toledo, Ohio
Toledo, Ohio
Duncan, Okla
Tulsa, Okla.
Marcus Hook, Penn.
Bakersfield, Calif.
Corpus Christi , Tex.
Bakersfield, Calif.
Chalmette, La.
Kenai , Alaska
Wolf Point, Mon.
Carrizo Springs, Tex.
Newcastle, Wy.
Wilmington, Calif.
Lawrenceville, 111.
Lockport, 111.
Convent, La.
Westville, N.J.
Anacortes, Wash.
Casper, Wy.
Port Arthur, Tex.
Amarillo, Tex.
El Paso, Tex.
West Tulsa, Okla.
Port Neches, Tex.
Fort Worth, Tex.
Texas City, Tex.
Commerce City, Colo.
Three Rivers, Tex.
Bloomfield, N. Mex.
Tonkawa, Okla.
Bakersfield, Calif.
Alma, Mich.
Tacoma, Wash.
/ 1 \
REFINERY11'
CAPACITY
(mVday)
954
1750
15900
52
3500
4130
36600
30200
6360
2230
716
.38200
26200
19100
19900
7710
14100
26200
1400
9060
191
15400
6040
398
2070
1670
11900
13400
11400
22300
14000
10000
3340
64600
3180
2700
7950
7470
477
9540
2780
238
338
954
4220
6500
2540

LUBES*1' ASPHALT*1'
(m'/day) (m3/day)
• --- 372
554
— —
— —
48
175
1320
1590 1750
207
1370
636
— —
334
1110
— —
— —
668
2700 1910
— —
— _--
— —
— —
— —
— —
— —
— —
— —
429
— —
— —
— —
— —
239
3180
— —
— —
— —
1430
— —
— —
— —
127 19
— —
— —
— —
477
>.. 477

COKE*1'
(metric tpd)


—
—
—
—
2000
—
—
—
—
• —
554
590
—
363
272
—
—
213
—
318
—
—
—
—
1500
—
272
—
—
—
114
—
91
91
—
—
—
—
—
—
—
—
191
—
...

OPERATING* '
GASOLINE
OUTPUT
(mVday)

—
3720
—
—
1160
21400
20300
1860
—
—
22800
8700
8700
13800
4390
6420
13500
151
4710
—
9810
—
—
—
477
11800
7080
5990
1230
5250
3550
1500
26200
1620
1510
3580
—
—
3550
2590
—
—
—
4300
3530
398

-------
              TABLE C-l — COMPLETE  LIST OF UNITED STATES REFINERIES  BY COMPANIES  (Continued)
                                                                                        PRODUCTION CAPACITY



230.
231.
232.
233.
234.
235.
236.
237.
238.
239.
240.
241.
242.
243.
0 2™'
V 245.
-o 246.
247.



COMPANY
Union Oil Co. of Calif.



Union Texas Petroleum
United Refining Co.
Valvoline Oil Co.
Vickcrs Petroleum
Vulcan Asphalt Ref.
Warrior Asphalt Co.
West Coast Oil Co.
Westco Refining Co.
Westland Oil Co.
Winston Refining
Wireback Oil Co.
Wolf's Head Oil Ref.
Yetter Oil Co.
Young Refining Corp.
TOTAL


LOCATION
Los Angeles, Calif.
San Francisco, Calif.
Lemont , 111.
Nederland, Tex.
Winnie, Tex.
Warren, Penn.
Freedom, Penn.
Ardmore, Okla.
Cordova, Ala.
Holt, Ala.
Bakersfield, Calif.
Cut Bank, Mon.
Williston, N.D.
Fort Worth, Tex.
Plymouth, 111.
Reno, Penn.
Colmar, 111.
Douglasvi lie, Ga.

/ 1 \
REFINERY1 U
CAPACITY
(mVday)
17200
17600
24200
18400
1510
6040
986
5000
477
385
2540
741
741
2390
238
334
159
398 '
2262854

LUBES^
(m3/day)

572
—
557
—
—
207
—
—
—
—
—
—
—
—
80
—
—
32531

ASPHALT*1*
(in'/day)
1590
978
318
859
— ' •
636
—
795
—
274
636
—
—
—
—
—
—
207
107073

COKE(1)
(metric tpd)

1680
908
—
—
—
—
—
—
. — •
—
—
—
—
—
—
—
—
39628
OPERATING^2*
GASOLINE
OUTPUT
(mVday)
8780
11100
11300
8060
1256
2290
—
2610
—
—
318
242
318
405
—
—

—
1052858
Source:   (1) "Annual Refining Survey," Oil & Gas J. 1  April 1974.
         (2) National Petroleum News, Fact Book, Mid-May  1974. N.Y., McGraw-Hill, 1974.

-------