U.S. PETROLEUM REFINING
`
`
`MEETING REQUIREMENTS FOR
`
`CLEANER FUELS AND REFINERIES
`
`VOLUME IV, PART 2-SUPPLY, DEMAND, AND LOGISTICS APPENDIX
`
`
`
`NATIONAL PETROLEUM COUNCIL
`AUGUST 1993
`
`FORD Ex. 1143, page 612
` IPR2020-00013
`
`

`

`COVER PHOTOGRAPH:
`REFINERY,
`CHEVRON
`U.S.A. INC.
`PASCAGOULA
`
`FORD Ex. 1143, page 613
` IPR2020-00013
`
`

`

`U.S. PETROLEUM REFINING
`
`
`MEETING REQUIREMENTS FOR
`
`CLEANER FUELS AND REFINERIES
`
`VOLUME IV, PART 2-SUPPLY, DEMAND, AND LOGISTICS APPENDIX
`
`
`
`NATIONAL PETROLEUM COUNCIL
`(OMMITIEE ON REFINING,
`KENNETH T. DERR, CHAIRMAN
`AugusT 1993
`
`,,>:-
`
`FORD Ex. 1143, page 614
` IPR2020-00013
`
`

`

`NATIONAL PETROLEUM COUNCIL
`Ray L. Hunt, Chairman
`Kenneth T. Derr, Vice Chairman
`Marshall W. Nichols, Executive
`Director
`U.S. DEPARTMENT OF ENERGY
`Hazel R. O'Leary, Secretary
`
`The National Petroleum Council is a federal
`
`
`
`advisory committee to the Secretary of Energy.
`
`The sole purpose of the National Petroleum Council
`
`
`is to advise, inform, and make recommendations to
`
`the Secretary of Energy on any matter requested
`
`
`by the Secretary relating to
`oil and natural gas or to the oil and gas industries.
`
`All Rights Reserved
`Library of Congress Catalog Card Number: 93-86296
`© National Petroleum Council1993
`Printed in the United States of America
`
`FORD Ex. 1143, page 615
` IPR2020-00013
`
`

`

`TABLE OF CONTENTS
`
`Appendix L: Appendix to Chapter Three -
`Supply, Demand, and Logistics
`
`Part 2
`
`Section VII: Refining Industry Modeling (Continued)
`
`VII-S: Summary Tables- Unit Capacity Information
`VII -6: Regional Investments
`- 1995 Model Year
`VII-7: Table- Bunker Fuel Outlook
`VII-8: Summary Tables-LP Case Comparisons (Foreign)
`
`VII -9: Pace Report on Foreign Refining Policy
`
`
`
`VII-10: (Foreign) Refinery Stationary Emission, Health and Safety
`(EHS)
`
`
`
`
`VII -11: EIA Integrated Petroleum Supply Reporting System
`
`Section VIII: Cost of U.S. and Foreign Produced Products
`
`VIII-1: Layer Cost Calculations
`VIII-2: Layered Cost Buildup (ABC) Tables
`
`
`
`
`VIII-3: Cost-Volume Relationships and Supplemental Material
`
`
`
`Section IX: Foundation Case Findings
`
`IX-1: Summary Regional/PADD Model Output Tables
`
`
`IX-2: Rationale for Small Changes in Variables
`
`FORD Ex. 1143, page 616
` IPR2020-00013
`
`

`

`FORD Ex. 1143, page 617
`IPR2020-00013
`
`FORD Ex. 1143, page 617
` IPR2020-00013
`
`

`

`Appendix L, Section VII-5
`
`Summary Tables - Unit Capacity Information
`
`This appendix tabulates the foreign regions' unit capacity for
`
`
`
`individual types of processing units. The increase in each unit type
`
`capacity is tabulated by region and ·covers the future years for the study.
`It is based on FC-1.
`
`FORD Ex. 1143, page 618
` IPR2020-00013
`
`

`

`FORD Ex. 1143, page 619
`IPR2020-00013
`
`FORD Ex. 1143, page 619
` IPR2020-00013
`
`

`

`REGION: CAN
`
`�
`I:""' � ......
`
`0
`
`0
`
`0
`28
`0
`
`0
`29
`0
`
`3
`
`0
`
`10 0
`
`0
`
`0 708 92
`35
`0 0 394 100
`0 0 1n 100
`0
`0
`28
`0
`0 46 100
`
`0
`0
`
`UNIT CAPACITY INFORMATION-FOREIGN
`DLF
`10122
`I 0 8127
`REV. 12/31
`06/16
`LP
`89 89 95-89 95-89 195 95
`00 10-00 10-00 110 10
`00-95 00-95 00
`YEAR
`-o -0 2034 76
`Delta %Change %Utili Delta %Change %Utili
`%Utili Delta %Change %Utili
`1851 78 183 10 203 4 77
`ATMOS. CRUDE DIS BPSD
`
`651 94 57 9 708 92
`BPSD
`VAC. DIST.
`372 100 22 6 394 100
`35
`35
`%VAC
`169 100 8 5 1n 100
`BPOD
`GOFCCU
`BPOD
`GO HYDROCRACKE
`BPOD
`GO THERMAL CRA
`BPOD
`%GO CONV.
`18 100 28 156 46 100
`BPOD
`RESIDFCCU
`0 0 23 100
`15 100 8 52 23 100
`BPOD
`RESID HYDROCRA
`0 0 21 100
`20 100 1 5 21 100
`BPOD
`DELA YEO COKER
`0
`0
`0
`BPOD
`FLUID COKER
`4
`BPOD
`FLEXICOKER
`40 86 87 100
`0 47 9
`47 100 0
`BPOD
`% RESID CONV.
`0
`0
`0
`0
`BPOD
`FCC NAPH SPLIT
`0 0 53 79
`50 100 4 7 53 52
`BPOD
`FCC DeC5
`0
`0
`0
`0
`BPOD
`VIS BREAKER
`0 0 114 100
`114 100 0 0 114 100
`BPOD
`SOLV. DEASPH.
`0 0 242 73
`242 46 0 0 242 81
`BPOD
`CCAEFORMER
`0 0 10 0
`0 0 10
`0
`BPOD
`LP SA REFORMER
`19 0 43 226 62 3
`BPOD
`C41SOM
`19 0 1 5 20 0
`BPOD
`C5/C61SOM
`35 100 1 3 36 100
`BPOD
`C3=POLY
`14 100 10 70 24 100
`BPOD
`HFALKY
`BPOD
`H2S04ALKY
`1 5 27 78
`26 0
`BPOD
`RESIDHDS
`353 53 55 15 408 53
`BPOD
`DISTHDS
`0
`0
`0
`BPOD
`FCC FEED HDS
`401 57 37 9 438 71
`BPOD
`NAPH HDS
`0
`0
`0
`BPOD
`MTBE
`0
`0
`0
`BPOD
`TAME
`300 91 86 29 386 79
`MMSC
`HYDROGEN
`
`0 62 16
`0
`0 20 0
`0
`0 36 100
`0
`0 0 24 100
`0 0 27 0
`0
`0 408 96
`0
`0
`0 0 438
`0
`0
`0 0 386 84
`
`0
`
`0
`4
`
`0
`
`LP INVEST ---
`
`MM$
`
`31
`
`69
`
`FORD Ex. 1143, page 620
` IPR2020-00013
`
`

`

`09/09
`I
`YEAR 89 89 95-89 95-89 195 95 OQ-95 oo-95 I oo 00 1Q-OO 1Q-OO 110 10
`I
`' ATMOS. CRUDE DIS BPSD 9178 88 687 7 9865 84 0 0 9865 83
`
`REGION: NWE LP 06/11
`
`12/10
`
`%Utili Delta %Change %Utili Delta %Change %Utili Delta %Change %Utili
`
`19
`
`VAC. DIST. BPSD 3800 87 72 2 3872 86 0 0 3872 84
`39
`39
`41
`%VAC
`BPOD 1273 100 156 12 1428 100 0 0 1428 100
`GOFCCU
`GO HYDROCRACKE BPOD 192 100 108 56 300 100 0 0 300 100
`GO THERMAL CRA BPOD 121 100 54 44 175 53 0 0 175 39
`19
`%GO CONV. BPOD 17
`0
`0
`0
`0
`BPOD 0
`RESID FCCU
`0
`0
`0
`0
`RESID HYDROCRA BPOD 0
`DELA YEO COKER BPOD 150 100 18 12 168 100 0 0 168 100
`0
`0
`0
`0
`FLUID COKER BPOD 0
`
`2
`
`2
`
`�
`r-"4
`� SOLV. DEASPH. BPOD 12 100 1 5 13 100 0 0 13 100
`
`FLEXICOKER BPOD 27 100 1 5 28 100 0 0 28 100
`FCC NAPH SPLIT BPOD 89 100 352 396 441 96 0 0 441 53
`FCC DeC5
`VISBREAKER BPOD 722 97 85 12 807 85 0 0 807 85
`CCREFORMER BPOD 517 100 128 25 645 100 -0 -0 645 100
`LP SR REFORMER BPOD 792 100 96 12 888 73 0 0 888 57
`C5/C61SOM BPOD 80 0 98 123 178 8 0 0 178 8
`BPOD 40 0 2 5 42 0 0 0 42 0
`C3=POLY
`11 100 56 509 67 100
`BPOD 91 100 36 40 127 100 0 0 127 100
`HFALKY
`H2S04ALKY BPOD 0
`11
`BPOD 1759 69 360 20 2119 69 140 7 2258 100
`BPOO 11 100 0 0 11 100 0 0 11 100
`RESID HDS
`DIST HDS
`FCC FEED HDS BPOD 692 100 35 5 726 100 0 0 726 100
`BPOD 1889 70 383 20 2272 58 0 0 2272 52
`NAPH HDS
`BPOD
`22 100 36 166 57 100
`22
`MTBE
`BPOD
`4 100
`4
`0
`TAME
`HYDROGEN
`MMSC 548 64 452 82 1000 68 0 0 1000 89
`MM$
`LP INVI;ST
`
`% RESID CONV. BPOD 2
`
`BPOD 0 0 0 0 0
`
`34
`
`34 100
`
`BPOD 18 0 4 22 22 0 0 0 22 100
`
`C41SOM
`
`1167
`
`FORD Ex. 1143, page 621
` IPR2020-00013
`
`

`

`100
`
`0
`17
`26
`0
`0
`
`�
`r-t
`�
`
`�
`
`REGION:MED LP
`07/07
`10/15
`110/02
`YEAR
`89
`89
`95-89
`95-89 195 95 00-95 00-95 00 00 10-00 10-00 10 10
`o/o Utili
`%Change o/o Utili Delta %Change o/o Utili Delta %Change o/o Utili
`Delta
`ATMOS. CRUDE DIS BPSD
`7226
`7 7727 66 -0 -0 7727 71
`71
`500
`VAC. DIST. BPSD
`1647
`100
`19 1962 100 -38 -2 1924 100
`315
`o/o VAC
`23
`25
`25
`GOFCCU
`BPOD
`570
`100
`147
`26 717 100 0 0 717 100
`GO HYDROCRACKE BPOD
`78
`100
`222
`283 300 100 0 0 300 100
`GO THERMAL CRA BPOD
`64
`100
`23
`36 87 12 0 0 87 12
`o/oGO CONV. BPOD
`10
`14
`14
`RESID FCCU
`BPOD
`0
`0
`0
`0
`RESID HYDROCRA BPOD
`0
`17
`17
`0
`DELA YEO COKER BPOD
`61
`43 87 100 0 0 87 100
`FLUID COKER BPOD
`0
`0
`0
`0
`FLEXICOKER BPOD
`0
`0
`0
`0
`o/o RESID CONV. BPOD
`1
`1
`1
`FCC NAPH SPLIT BPOD
`263
`100
`23 325 100 98 30 422 86
`62
`59
`FCC DeC5
`59
`BPOD
`0
`0
`0
`0
`-4
`VIS BREAKER
`100
`BPOD
`328
`-1 324 100 0 0 324 100
`SOLV. DEASPH. BPOD
`0
`0
`0
`0
`0
`CCREFORMER BPOD
`100
`163
`16 189 100 0 0 189 100
`26
`
`LP SR REFORMER BPOD 628
`67
`0 628 59 0 0 628 59
`0
`C41SOM
`BPOD
`16
`0
`2
`13 18 0 0 0 18 0
`49
`C5/C61SOM BPOD
`50
`0
`98 99 4 0 0 99 17
`C3=POLY
`5
`BPOD
`0
`82 9 0 0 0 9 0
`4
`HFALKY
`36
`BPOD
`100
`0 36 100 0 0 36 100
`0
`100 22 100 35 157 57 100
`H2S04ALKY
`BPOD
`100
`11
`11
`RESID HDS
`BPOD
`0
`30 100 89 291 119 100
`30
`DISTHDS
`BPOD
`1020
`83
`8 1103 80 357 32 1460 100
`85
`FCC FEED HDS BPOD
`57
`5 60 100 0 0 60 100
`100
`3
`NAPH HDS
`BPOD
`967
`62
`10 1065 53 0 0 1065 58
`98
`MTBE
`BPOD
`15
`15 100 14 92 28 100
`TAME
`BPOD
`0
`0
`7
`7 100
`626 105 594
`286 594
`154
`440
`
`HYDROGEN MMSC
`
`LP INVEST MM$
`
`7 ---
`
`-----
`
`_136_g_ -·
`
`---
`
`FORD Ex. 1143, page 622
` IPR2020-00013
`
`

`

`�
`L4 �
`
`J:..
`
`REGION: ME
`
`LP 06/29
`10/04
`12113
`YEAR 89 89 95-89 95-89 95 95 00-95 00-95 00 00 1Q-OO 10-00 10 10
`
`I 09/23
`%Utili Delta %Change %Utili Delta % Chana e %Utili Delta %Change %Utili
`
`ATMOS. CRUDE DIS BPSD 5000 91 1594 32 6594 76 0 0 6594 80 0 0 6594 86
`BPSD 1509 73 349 23 1858 77 -0 -0 1858 73 0 0 1858 94
`VAC. DIST.
`%VAC
`30
`28
`28
`28
`GOFCCU
`BPOD 182 100 66 36 248 100 0 0 248 100 283 114 531 100
`GO HYDROCRACKE BPOD 326 100 109 33 434 100 0 0 434 100 0 0 434 100
`GO THERMAL CRA BPOD 0
`0
`0
`0
`0
`0
`0
`%GO CONV. BPOD 10
`10
`10
`15
`0
`RESID FCCU
`BPOD 0
`0
`0
`0
`0
`0
`RESID HYDROCRA BPOD 0
`0
`0
`0
`0
`0
`0
`DELA YEO COKER BPOD 60 100 3 5 63 100 0 0 63 100 0 0 63 100
`0
`FLUID COKER BPOD 0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`1
`1
`1
`26 100 44 171 69 62 172 249 241 100
`FCC DeC5
`0
`0
`102
`102 100
`VISBREAKER BPOD 243 19 81 33 324 11 0 0 324 54 0 0 324 100
`0
`0
`0
`0
`0
`0
`
`% RESID CONV. BPOD 1
`
`FLEXICOKER BPOD 0
`FCC NAPH SPLIT BPOD . 0 0 26
`BPOD 25 0 -25 -100 0
`SOLV. DEASPH. BPOD 0
`CCREFORMER BPOD . 122 100 99 81 221 100 0 0 221 100 30 13 251 100
`LP SR REFORMER BPOD 326 50 48 15 374 82 0 0 374 100 0 0 374 100
`BPOD 0
`BPOD 1 100 0 0 1 100 0 0 1 0 0 0 1 0
`C3=POLY
`
`0
`C41SOM
`0
`0
`0
`0
`0
`C5/C61SOM BPOD 3 0 51 1821 54 0 0 0 54 48 0 0 54 48
`
`BPOD 12 100 2 17 14 100 0 0 14 100 0 0 14 100
`HFALKY
`BPOD 0
`H2S04ALKY
`3
`3 100 11 350 14 100 55 404 68 100
`433 100
`BPOD 0
`0
`RESID HDS
`0
`215
`215 100 218
`BPOD 555 79 242 44 797 100 230 29 1026 100 289 28 1315 100
`DISTHDS
`FCC FEED HDS BPOD 0 67 32
`32 100 38 119 69 100 0 0 69 100
`BPOD 507 60 186 37 694 78 0 0 694 94 0 0 694 100
`NAPH HDS
`BPOD
`MTBE
`5 100 -2 -38' 3 100 2 61 5 100
`5
`0
`0
`0
`0
`0
`0
`
`BPOD
`TAME
`HYDROGEN MMSC 1299 64 107 8 1406 79 0 0 1406 94 113 8 1519 100
`-----
`LPINVEST MM$
`
`1465
`
`4263
`
`FORD Ex. 1143, page 623
` IPR2020-00013
`
`

`

`�
`t"""4
`�
`I 01
`01
`
`REGION: LAT
`
`12104
`LP 06/23
`12/16
`10/02
`YEAR 89 89 95-89 95-89 195 95 00-95 00-95 00 0 0 10-00 10-00 10 10
`o/o Utili Delta %Change o/o Utili Delta o/o Change o/o Utili Delta o/o Change o/o Utili
`ATMOS. CRUDE DIS BPSD 7068 77 1148 16 8216 73 0 0 8216 82 0 0 8216 98
`BPSD 3005 67 626 21 3631 69 0 0 3631 91 0 0 3631 98
`VAC. DIST.
`o/o VAC
`44
`44
`43
`44
`BPOD 1071 100 292 27 1362 100 295 22 1657 100 359 22 2016 100
`GOFCCU
`GO HYDROCRACKE BPOD 22 100 179 833 201 100 0 0 201 100 0 0 201 100
`0
`0
`0
`GO THERMAL CRA BPOD 0
`0
`27
`23
`o/oGO CONV. BPOD 15
`0
`0
`BPOD 0
`RESID FCCU
`
`0
`
`0
`
`0
`
`FLUID COKER BPOD 0
`
`0
`
`o/o RESID CONV. BPOD 2
`
`3
`
`0
`
`0
`
`3
`
`0
`
`3
`
`0
`0
`19
`0
`RESID HYDROCRA BPOD 16 100 17 104 33 100 0 0 33 100 0 0 33 100
`DELAYED COKER BPOD 92 100 99 107 191 100 0 0 191 100 0 0 191 100
`0
`0
`FLEXICOKER BPOD 42 100 2 5 44 100 0 0 44 100 0 0 44 100
`FCC NAPH SPLIT BPOD 111 100 179 161 290 100 140 48 429 89 0 0 429 87
`0
`BPOD 371 100 217 58 587 100 0 0 587 54 0 0 587 100
`
`BPOD 28 100 3 11 31 100 0 0 31 100 0 0 31 100
`H2S04ALKY BPOD 49 100 1 2 50 100 168 339 218 100 1 0 219 100
`BPOD 765 60 331 43 1097 67 0 0 1097 100 92 8 1189 100
`BPOD 491 84 37 7 527 100 76 14 604 100 205 34 809 100
`11 100 20 190 30 100 -0 -0 30 100
`
`BPOD 0
`
`0
`
`0
`
`0
`
`RESID HDS
`DIST HDS
`FCC FEED HDS BPOD 409 100 33 8 442 100 0 0 442 100 0 0 442 100
`N APH HDS
`11
`BPOD
`MTBE
`18 100
`6 100 12
`6
`0
`0
`BPOD
`TAME
`HYDROGEN MMSC 350 77 400 114 750 82 0 0 750 94 0 0 750 77
`
`0
`
`0
`
`0
`
`LP INVEST MM$
`
`3292
`
`3699
`
`BPOD 0 0 0
`
`51
`
`51 100 111 218 162 100
`
`FCC DeC5
`VIS BREAKER
`SOLV. DEASPH. BPOD 110 100 37 34 147 100 0 0 147 100 0 0 147 100
`CCREFORMER BPOD 47 100 0 0 47 100 23 50 70 100 176 251 246 100
`LP SR REFORMER BPOD 395 76 28 7 423 90 0 0 423 100 0 0 423 100
`BPOD 28 100 1 4 29 0 0 0 29 100 0 0 29 100
`C41SOM
`C5/C61SOM BPOD 13 100 18 138 31 0 0 0 31 100 0 0 31 100
`BPOD 15 100 0 0 15 100 0 0 15 0 0 0 15 0
`C3=POLY
`HFALKY
`
`FORD Ex. 1143, page 624
` IPR2020-00013
`
`

`

`REGION: PAC
`
`�
`t"-1 �
`01 I 0"\
`
`112/08
`09/29
`LP 09/25
`12122
`95-89 95-89 95 95
`00-95 00-95 00 00 10-00 10-00 10 10
`YEAR 89 89
`%Utili
`Delta %Change %Utili Delta %Change %Utili
`Delta %Change %Utili
`0 0 11999 92 478 4 12477 100
`1902 19 11999 79
`BPSD 10097 78
`ATMOS. CRUDE DIS
`548 18 3556 74
`0 0 3556 76 76 2 3632 83
`BPSD 3008 78
`VAC. DIST.
`30
`30
`30
`29
`%VAC
`22 2 1264 100 255 20 1519 100
`403 48 1242 100
`BPOD 839 100
`GOFCCU
`0 0 454 100 463 102 917 100
`165 57 454 100
`BPOD 288 100
`GO HYDROCRACKE
`3 5 71 0
`0 0 71 0 0 0 71 100
`BPOD 68 0
`GOTHERMAL CRA
`15
`15
`20
`BPOD 12
`o/oGO CONV.
`0 0 90 100 0 0 90 100
`90 100
`90
`BPOD 0
`RESID FCCU .
`0
`0
`0
`0
`0 100
`0
`BPOD 0
`RESID HYDROCRA
`0 0 171 100 101 59 272 100
`57 50 171 100
`BPOD 114 100
`DELAYED COKER
`0
`0
`0
`0
`0
`BPOD 0
`0
`FLUID COKER
`0
`0
`0
`0
`0
`BPOD 0
`0
`FLEXICOKER
`0 2
`0 3
`0 2
`BPOD 1
`% RESID CONV.
`361 112 683 100 300 44 983 70
`40 14 322 100
`BPOD 282 100
`FCC NAPH SPLIT
`0
`0
`0
`0
`0
`BPOD 0 0
`0
`FCC DeC5
`0 0 359 100 44 12 403 100
`99 38 359 100
`BPOD 260 100
`VIS BREAKER
`0 0 68 100 0 0 68 100
`37 117 68 100
`BPOD 31 0
`SOLV. DEASPH.
`0 0 352 100 10 3 362 100
`145 70 352 100
`BPOD 207 100
`CCREFORMER
`0 0 1101 82 0 0 1101 100
`359 48 1101 69
`BPOD 742 71
`LP SR REFORMER
`0
`0
`0
`0
`0
`0
`BPOD 0
`C41SOM
`0 0 61 56 246 407 307 100
`33 116 61 0
`BPOD 28 0
`C5/C61SOM
`0 0 19 51 0 0 19 89
`2 12 19 0
`BPOD 17 0
`C3=POLY
`0 0 46 100 0 0 46 100
`19 73 46 100
`BPOD 27 100
`HFALKY
`124 290 166 100 24 14 190 100
`13 43 43 100
`H2S04ALKY
`281 80 630 99
`0 0 630 100 0 0 630 100
`RESID HDS
`768 47 2393 53
`0 0 2393 81 -0 -0 2393 100
`DISTHDS
`-1 -0 935 23 -99 -11 836 11
`196 27 936 21
`FCC FEED HDS
`544 45 1752 64
`0 0 1752 73 -0 -0 1752 100
`NAPH HDS
`21 240 30 100 2 5 31 100
`MTBE
`9
`0
`0
`0
`0
`0
`TAME
`0
`391 33 1582 75
`0 0 1582 78 56 4 1638
`HYDROGEN
`
`BPOD · 30 100
`
`BPOD 349 93
`BPOD 1625 29
`BPOD 740 14
`BPOD 1209 61
`BPOD
`BPOD
`MMSC 1191 47
`
`9 100
`
`LP INVEST
`
`MM$
`
`876
`
`5699
`
`FORD Ex. 1143, page 625
` IPR2020-00013
`
`

`

`Appendix L, Section VII-6
`
`Regional Investments-1995 Model Year
`
`INVESTMENT ASSUMPTIONS
`• All process unit investments were per the Facilities
`Task Group {FTG)
`
`
`except for the following which FTG did not develop:
`
`
`- Used Pace data for flexicoker, fluid coker, visbreaker, semi-regen
`C4 Isom, C3 Poly, HF I Alky, resid Hdc, resid Hds, sat gas plant,
`reformer,
`residFCC.
`
`
`- Assumed SDA to be same investment cost as visbreaker.
`• FCC and coker investments unsat gas plant investment
`.dQ. include
`
`requirements.
`• Crude, CCR and hydrocracking investments
`do nQ1 include
`
`any funds for
`
`sat gas plant, which must be added separately.
`
`on sulfur plant feed to estimate sulfur plant capacity
`
`Assumed increase in sat gas plant feed (1995 vs. 1989) in LP runs corresponds
`
`
`
`to new capacity added on calendar day basis (90% of stream day capacity).
`• Parallel assumption
`
`addition.
`• All new capacity added between 1989 and 1995 in Northwest Europe,
`Med,
`in existing refineries
`{FTG
`
`and Canada regions assumed to be retrofits
`estimate basis). For Pac Rim, Latin America, and Middle East refining
`in this period,
`regions
`
`
`20% of capital additions were estimated/ assumed to
`be part of grass roots refineries.
`• Per FTG, offsites plus other one-time costs (site prep, startup, etc.) at 65% of
`
`
`onsites for retrofit capacity (total investment= 1.65 x onsites) and 100% of
`
`
`
`
`onsites for grass roots capacity (total investment= 2.00 x onsites).
`• Area construction factors per FTG.
`
`
`• Annual ROI factor of .24 (applied
`to total capital costs) consists of .172 for
`
`
`
`10% DCF on investment plus .068 to cover fixed cash operating costs.
`• Refinery production of hydrocarbon
`MJDN noted in the attachments and
`
`
`
`used in deriving cents/gallon costs are based on Foundation Case 1 (FC-1)
`LP runs for each region.
`
`APP L.Vll.6-1
`
`FORD Ex. 1143, page 626
` IPR2020-00013
`
`

`

`• Year 1995 investments are assumed to be underway or sunk, and not
`
`
`
`
`changeable. Therefore, total annual costs in$ Billion developed for FC-1
`
`
`are assumed to be applicable to FC-2 and FC-3 also. (Results in unit costs
`
`for FC-2 and FC-3 higher than FC-1 because of the smaller demand
`divisors.)
`• Attached estimates
`do not include remedial or catch-up foreign refinery
`
`
`
`
`
`
`(stationary) emission investments or costs. These have been developed
`separately.
`
`APP L.VTI.6-2
`
`FORD Ex. 1143, page 627
` IPR2020-00013
`
`

`

`Appendix 3.VII-6
`February 4, 1993
`
`TABLE APP.L.VII.6-1
`
`FOREIGN REGIONS
`
`
`
`FACILITIES COST -1 995 MODEL YEAR
`
`Total
`Investment
`$Millions
`
`Annualized Invest/Fixed Optg. Costs*
`
`
`
`$MillionNr. Cents/Gal. MJDN
`
`Canada
`
`NWE
`
`Med
`
`1455
`
`7000
`
`4442
`
`Middle East
`
`5009
`
`Latin America
`
`7879
`
`Pac Rim
`
`11918
`
`349
`
`1680
`
`1066
`
`1202
`
`1884
`
`2860
`
`1.55
`
`1.64
`
`2.01
`
`2.42
`
`2.90
`
`2.58
`
`*
`
`Equates to total investment x 0.24 annualized factor for 1 0% ROI plus
`
`
`
`fixed operating costs on new facilities.
`
`APP L.VII.6-3
`
`FORD Ex. 1143, page 628
` IPR2020-00013
`
`

`

`Appendix 3. Vll-6
`
`February 4, 1993
`
`TABLE APP.L.VII.6-2
`
`1995 MODEL YEAR-FACILITY COSTS
`
`REGION - CANADA
`
`'95 Cap '89Cap '95-'89 W/S Unit W/S Unit W/S Unit Onsite
`TBD $MM/TBD $MM
`TBD $MM
`TBD
`TBD
`
`2,033.7 1,851.3 182.4 50
`150
`Atm Crude
`707.9 660.9 47.0 25
`44
`Vac Crude
`103.0 85.0 18.0 16.2 20
`SatG.P.
`393.6 372.0 21.6 150
`70
`FCC
`0.0 275
`70
`Resid FCC
`177.3 168.9 8.4 110
`30
`Hdc
`45.8 17.9 27.9 145
`30
`Resid Hdc
`22.5 14.8 7.7 110
`25
`
`Delayed Coker
`21.2 20.2 1.0 120
`25
`Fluid Coker
`0.0 201
`25
`Flex Coker
`37
`0.0
`25
`Thermal Cracker
`27
`25
`53.3 49.8 3.5
`Visbreaker
`27
`0.0
`25
`SDA
`113.6 113.6 0.0
`50
`35
`CCR
`26
`242.1 242.1 0.0
`20
`PTR
`10.1 10.1 0.0 17.5 10
`C41som
`15
`62.0 10.0 52.0 25
`C5/C61som
`19
`55
`20.4 19.4 1.0
`C3 Poly
`35.7 34.7
`55
`19
`1.0
`HFAiky
`19
`24.2 14.2 10.0 55
`H2S04Aiky
`27.3 26.0 1.3
`35
`65
`Resid Hds
`408.1 353.4 54.7 25
`30
`Dist Hds
`40
`0.0
`35
`FCC Fd Hdt
`10
`0.0
`2
`0.0
`MTBE
`437.5 400.5 37.0 45
`35
`Naphtha Hds
`
`Hydrogen Pit, MMSCF 386.0 300.0 86.0 50
`60
`1398.0 1030.0 368.0 20
`222
`
`Sulfur Pit, L TID
`
`0.33 60.8
`0.57 26.7
`0.81 14.6
`2.14 46.3
`3.93
`0.0
`3.67 30.8
`4.83 134.9
`4.40 33.9
`4.80
`4.8
`8.04
`0.0
`0.0
`1.48
`1.08
`3.8
`1.08
`0.0
`1.43
`0.0
`1.30
`0.0
`1.75
`0.0
`1.67 86.7
`2.89
`2.9
`2.9
`2.89
`2.89 28.9
`2.4
`1.86
`0.83 45.6
`1.14
`0.0
`5.00
`0.0
`1.29 47.6
`0.83 71.7
`0.09 33.2
`
`Total Onsite
`
`Offsite Factor (Retrofit)
`
`Offsite Factor (Grass Roots)
`Grass Roots Share
`
`Weighted Offsite Factor
`OnSite
`$MM
`
`+ Offsite,
`
`Area Factor
`
`Tot. Region Invest. $MM
`
`MBD *
`Region MJDN Production,
`
`$Invest/Daily Bbl MJDN
`ROI Factor
`
`Capital Charge
`
`$1881 MJDN
`¢/Gal MJDN
`
`678.3
`0.65
`1.0
`0.0
`0.65
`1119.1
`
`1.3
`1454.9
`
`1467.0
`2.72
`0.24
`
`0.65
`1.55
`
`* FC-1 reference
`
`
`
`case hydrocarbon MJDN volumes
`
`
`
`02-Jun-93 Revised
`
`APP L.Vll.6-4
`
`FORD Ex. 1143, page 629
` IPR2020-00013
`
`

`

`Appendix 3. Vll-6
`
`February 4, 1993
`
`TABLE APP.L.VI1.6-3
`
`1995 MODEL YEAR-FACILITY COSTS
`
`REGION -NW EUROPE
`
`'95 Cap '89 Cap '95-'89 W/S Unit W/S Unit W/S Unit On site
`TBD $MM
`TBD $MM/TBD $MM
`TBD
`TBD
`
`150
`9,864.6 9,178.1 686.5 50
`Atm Crude
`44
`3871.7 3310.3 561.4 25
`VacCrude
`20
`333.0 286.0 47.0 16.2
`Sat G.P.
`70
`1428.1 1272.5 155.6 150
`FCC
`70
`0.0 275
`Resid FCC
`299.7 192.1 107.6 110
`30
`Hdc
`30
`0.0 145
`Resid Hdc
`25
`167.9 150.4 17.5 110
`Delayed Coker
`25
`0.0 120
`Fluid Coker
`25
`27.9 26.6 1.3 201
`Flex Coker·
`25
`Thermal Cracker 174.8 121.3 53.5 37
`806.6 721.5 85.1 27
`25
`Visbreaker
`27
`25
`13.0 12.4 0.6
`.SDA
`35
`645.2 517.2 128.0 50
`CCR
`20
`887.9 791.9 96.0 26
`PTA
`21.9 17.9 4.0 17.5 10
`C41som
`15
`178.0 80.0 98.0 25
`C5/C61som
`19
`55
`41.8 39.8 2.0
`C3 Poly
`19
`126.9 90.9 36.0 55
`HFAiky
`19
`11.0 55
`11.0
`H2S04Aiky
`35
`65
`10.8 10.8 0.0
`Resid Hds
`2118.5 1758.6 359.9 25
`30
`Dist Hds
`726.1 691.5 34.6 40
`35
`FCC Fd Hdt
`0.0 21.5 10
`2
`21.5
`MTBE
`2271.7 1889.2 382.5 45
`35
`Naphtha Hds
`
`Hydrogen Pit, MMSCF 603.4 548.0 55.4 50
`60
`222
`5725.0 4778.0 947.0 20
`
`Sulfur Pit, LT/D
`
`0.33 228.8
`0.57 319.0
`38.1
`0.81
`2.14 333.4
`0.0
`3.93
`3.67 394.5
`0.0
`4.83
`77.0
`4.40
`0.0
`4.80
`10.5
`8.04
`79.2
`1.48
`91.9
`1.08
`0.6
`1.08
`1.43 182.9
`1.30 124.8
`7.0
`1.75
`1.67 163.3
`5.8
`"2.89
`2.89 104.2
`31.8
`2.89
`0.0
`1.86
`0.83 299.9
`39.5
`1.14
`5.00 107.5
`1.29 491.8
`46.2
`0.83
`85.3
`0.09
`
`Total Onsite
`
`Offsite Factor (Retrofit)
`
`Offsite Factor (Grass Roots)
`Grass Roots Share
`
`Weighted Offsite Factor
`$MM
`OnSite
`
`+ Offsite,
`
`Area Factor
`
`Tot. Region Invest. $MM
`
`MBD *
`Region MJDN Production,
`
`$ Invest/Daily Bbl MJDN
`ROI Factor
`
`Capital Charge
`
`$1881 MJDN
`¢/Gal MJDN
`
`* FC-1 reference
`
`
`case hydrocarbon MJDN volumes
`
`
`
`02-Jun-93 Revised
`
`APP L.VII.6-5
`
`3263.1
`0.65
`1.0
`0.0
`0.65
`5384.1
`
`1.3
`6999.3
`
`6674.0
`2.87
`0.24
`
`0.69
`1.64
`
`FORD Ex. 1143, page 630
` IPR2020-00013
`
`

`

`Appendix 3.VII-6
`
`February 4, 1993
`
`TABLE APP.L.VII.6-4
`
`1995 MODEL YEAR-FACILITY COSTS
`
`REGION -MED.
`
`'95 Cap '89 Cap '95-'89 W/S Unit W/S Unit W/S Unit
`Onsite
`T BD
`T BD
`T BD
`$MM
`T BD
`$MM/TBD $MM
`
`7,226.3
`7,726.6
`1745.5
`2158.0
`191.0
`205.0
`716.8 570.1
`
`500.3
`Atm Crude
`50
`412.5
`25
`Vac Crude
`14.0
`16.2
`Sat G.P.
`146.7
`150
`FCC
`275
`0.0
`Resid FCC
`221.9
`110
`Hdc
`17.1
`145
`Resid Hdc
`110
`26.0
`Delayed Coker
`120
`0.0
`Fluid Coker
`201
`0.0
`Flex Coker
`37
`23.2
`Thermal Cracker
`-3.8 27
`Visbreaker
`27
`0.0
`SDA
`26.0
`50
`188.7
`CCR
`26
`0.0
`628.3
`PTA
`17.5
`2.0
`17.5
`C41som
`49.0
`25
`98.9
`C5/C61som
`4.0
`55
`8.9
`C3 Poly
`55
`0.0
`35.9
`HFAiky
`11.0
`55
`22.0
`H2S04Aiky
`65
`30.4
`30.4
`Resid Hds
`25
`1102.8 1019.8 83.0
`Dist Hds
`40
`2.8
`56.9
`59.7
`FCC Fd Hdt
`10
`14.6
`0.0
`14.6
`MTBE
`45
`98.4
`967.0
`1065.4
`Naphtha Hds
`50
`81.7
`154.0
`Hydrogen Pit, MMSCF 235.7
`20
`4036.0 2731.0 1305.0
`Sulfur Pit, LT/D
`
`150
`44
`20
`70
`70
`30
`30
`25
`25
`25
`25
`25
`25
`35
`20
`10
`15
`19
`19
`19
`35
`30
`35
`2
`35
`60
`222
`
`0.33
`166.8
`0.57
`234.4
`0.81
`11.3
`2.14
`314.4
`3.93
`0.0
`3.67
`813.6
`4.83
`82.7
`4.40 114.4
`4.80
`0.0
`8.04
`0.0
`1.48
`34.3
`1.08
`-4.1
`1.08
`0.0
`1.43
`37.1
`1.30
`0.0
`3.5
`1.75
`1.67
`81.7
`11.6
`2.89
`2.89
`0.0
`2.89
`31.8
`1.86
`56.5
`69.2
`0.83
`1.14
`3.2
`73.0
`5.00
`1.29
`126.5
`68.1
`0.83
`117.6
`0.09
`
`2447.5
`0.65
`1.0
`0.0
`0.65
`4038.3
`
`1.1
`4442.2
`
`3467.0
`3.51
`0.24
`
`0.84
`2.01
`
`300.2
`17.1
`86.6
`
`87.1
`324.4
`
`78.3
`
`60.6
`
`63.9
`328.2
`
`162.7
`628.3
`15.5
`49.9
`4.9
`35.9
`11.0
`
`Total Onsite
`
`Offsite Factor ( Retrofit)
`Offsite Factor (Grass Roots)
`Grass Roots Share
`
`
`Weighted Offsite Factor
`$MM
`OnSite
`
`+ Offsite,
`
`Area Factor
`$MM
`Tot. Region Invest.
`
`MBD *
`Region MJDN Production,
`
`$ Invest/Daily Bbl MJDN
`ROI Factor
`
`Capital Charge
`
`$1881 MJDN
`¢/Gal MJDN
`
`• FC-1 reference
`
`
`
`case hydrocarbon MJDN volumes
`
`02-Jun-93 Revised
`
`APP L. VTI.6-6
`
`FORD Ex. 1143, page 631
` IPR2020-00013
`
`

`

`Appendix 3.VII-6
`
`
`February 4, 1993
`
`TABLE APP.L.VII.6-5
`
`1995 MODEL YEAR -FACILITY COSTS
`
`REGION -MID. EAST
`
`'95 Cap '89 Cap '95-'89 W/S Unit W/S Unit W/S Unit Onsite
`T BD
`$MM
`T BD
`T BD
`T BD
`$MMITBD $MM
`
`6,594.0
`1858.1
`211.0
`248.0
`
`434.3
`
`63.4
`
`Atm Crude
`Vac Crude
`SatG.P.
`FCC
`Resld FCC
`Hdc
`Resld Hdc
`Delayed Coker
`Fluid Coker
`Flex Coker
`Thermal Cracker
`Vlsbreaker
`SDA
`CCR
`PTA
`C41som
`C5/C61som
`C3 Poly
`HFAiky
`H2S04 Aiky
`Resld Hds
`796.9
`DistHds
`31.5
`FCCFdHdt
`5.3
`MTBE
`693.7
`Naphtha Hds
`Hydrogen Pit, MMSCF 1406.0
`4329.0
`Sulfur Pit, LT/D
`
`324.4
`
`221.3
`374.2
`
`53.8
`1.2
`14.0
`3.0
`
`325.5
`
`60.4
`
`243.2
`
`5,000.0 1594.0
`50
`25
`349.4
`1508.7
`38. 0 16.2
`173.0
`150
`181.9
`66.1
`275
`0.0
`108.8 110
`145
`0.0
`110
`3.0
`120
`0.0
`201
`0.0
`37
`0.0
`27
`81.2
`27
`0.0
`50
`122.3
`99.0
`26
`326.2 48.0
`17.5
`0.0
`25
`51.0
`55
`0.0
`55
`2.0
`55
`3.0
`65
`0.0
`25
`241.8
`40
`31.5
`10
`5.3
`0.0
`45
`186.4
`507.3
`50
`107.0
`1299.0
`20
`2900.0 1429.0
`
`2.8
`1.2
`12.0
`
`555.1
`
`Total Onsite
`
`Offslte Factor (Retrofit)
`Offslte Factor (Grass Roots)
`Grass Roots Share
`
`
`Weighted Offsite Factor
`$MM
`
`Area Factor
`
`Tot. Region Invest. $MM
`
`OnSite + Offsite,
`MBD *
`
`Region MJDN Production,
`
`$ Invest/Daily Bbl MJDN
`ROI Factor
`
`Capital Charge
`
`$/BBIMJDN
`¢/Gal MJDN
`
`* FC-1 reference
`
`
`
`case hydrocarbon MJDN volumes
`
`
`
`02-Jun-93 Revised
`
`APP L.VIT.6-7
`
`150
`44
`20
`70
`70
`30
`30
`25
`25
`25
`25
`25
`25
`35
`20
`10
`15
`19
`19
`19
`35
`30
`35
`2
`35
`60
`222
`
`0.33
`531.3
`198.5
`0.57
`0.81
`30.8
`2.14
`141.6
`0.0
`3.93
`3.67 398.9
`0.0
`4.83
`13.2
`4.40
`0.0
`4.80
`0.0
`8.04
`0.0
`1.48
`87.7
`1.08
`0.0
`1.08
`141.4
`1.43
`62.4
`1.30
`0.0
`1.75
`85.0
`1.67
`0.0
`2.89
`5.8
`2.89
`8.7
`2.89
`0.0
`1.86
`201.5
`0.83
`36.0
`1.14
`26.5
`5.00
`239.7
`1.29
`89.2
`0.83
`128.7
`0.09
`
`2427.0
`0.65
`1.0
`0.2
`0.72
`4174.4
`
`1.2
`5009.3
`
`3240.0
`4.24
`0.24
`
`1.02
`2.42
`
`FORD Ex. 1143, page 632
` IPR2020-00013
`
`

`

`Appendix 3.VII-6
`
`February 4, 1993
`
`TABLE APP.L.VII.6-6
`
`1995 MODEL YEAR· FACILITY COSTS
`
`REGION· LATIN AMER.
`
`'95 Cap '89Cap '95-'89 W/S Unit W/S Unit W/S Unit Onsite
`TBD $MM
`TBD $MM/TBD $MM
`TBD
`TBD
`
`150
`8,215.5 7,067.6 1147.9 50
`Atm Crude.
`3631.3 3005.0 626.3 25
`44
`VacCrude
`156.0 106.0 50.0 16.2 20
`SatG.P.
`70
`1362.0 1070.5 291.5 150
`FCC
`70
`0.0 275
`Resid FCC
`30
`200.6 21.5 179.1 110
`Hdc
`33.0 16.2 16.8 145
`30
`Resid Hdc
`190.7 92.1 98.6 110
`25
`
`Delayed Coker
`25
`0.0 120
`Fluid Coker
`43.9 41.9 2.0 201
`25
`Flex Coker
`37
`25
`0.0
`Thermal Cracker
`587.3 370.8 216.5 27
`25
`Visbreaker
`146.0 109.5 36.5 27
`25
`SDA
`46.7 46.7 0.0
`50
`35
`CCR
`20
`422.8 394.8 28.0 26
`PTR
`29.2 28.2 1.0 17.5 10
`C41som
`31.0 13.0 18.0 25
`15
`C5/C61som
`19
`55
`14.6 14.6 0.0
`C3Poly
`19
`55
`30.8 27.8 3.0
`HFAiky
`55
`19
`49.7 48.7 1.0
`H2S04Aiky
`65
`0.0
`35
`Resid Hds
`1096.6 765.3 331.3 25
`30
`Dist Hds
`441.5 409.0 32.5 40
`35
`FCC Fd Hdt
`0.0 10.5 10
`2
`10.5
`MTBE
`527.4 490.9 36.5 45
`35
`Naphtha Hds
`60
`
`Hydrogen Pit, MMSCF 685.0 350.0 335.0 50
`222
`4972.0 3126.0 1846.0 20
`
`Sulfur Pit, L TID
`
`0.33 382.6
`0.57 355.9
`40.5
`0.81
`2.14 624.6
`0.0
`3.93
`3.67 656.7
`4.83
`81.2
`4.40 433.8
`0.0
`4.80
`16.1
`8.04
`0.0
`1.48
`1.08 233.8
`39.4
`1.08
`0.0
`1.43
`36.4
`1.30
`1.8
`1.75
`30.0
`1.67
`0.0
`2.89
`8.7
`2.89
`2.9
`2.89
`0.0
`1.86
`0.83 276.1
`37.1
`1.14
`52.5
`5.00
`46.9
`1.29
`0.83 279.2
`0.09 166.3
`
`Total Onsite
`
`Offsite Factor (Retrofit)
`
`Offsite Factor (Grass Roots)
`Grass Roots Share
`
`Weighted Offsite Factor
`OnSite
`$MM
`
`Area Factor
`Tot. Region Invest. $MM
`
`
`+ Offsite,
`MBD *
`
`Region MJDN Production,
`
`$ Invest/Daily Bbl MJDN
`ROI Factor
`
`Capital Charge
`
`$/881 MJDN
`¢/Gal MJDN
`
`* FC-1 reference
`
`
`
`case hydrocarbon MJDN volumes
`
`
`
`02-Jun-93 Revised
`
`APP L.Vll.6-8
`
`3802.5
`0.65
`1.0
`0.2
`0.72
`6540.4
`
`1.2
`7848.5
`
`4233.0
`5.08
`0.24
`
`1.22
`2.90
`
`FORD Ex. 1143, page 633
` IPR2020-00013
`
`

`

`Appendix 3.VII-6
`
`
`February 4, 1993
`
`TABLE APP.L.VII.6-7
`
`1995 MODEL YEAR-FACILITY COSTS
`REGION -PACIFIC RIM
`
`'95 Cap '89 Cap '95-'89 W/S Unit W/S Unit W/S Unit On site
`TBD
`TBD $MM/TBD $MM
`TBD
`TBD
`$MM
`
`288.4
`
`171.0
`
`113.7
`
`11,998.7 10,097.0 1901.7
`50
`Atrn Crude
`25
`3008.0
`548.3
`3556.3
`Vac Crude
`16.2
`114.0
`259.0
`373.0
`SatG.P.
`150
`1242.0
`838.7
`403.3
`FCC
`275
`90.0
`90.0
`Resid FCC
`110
`453.7
`165.3
`Hdc
`145
`0.0
`Resid Hdc
`110
`57.3
`Delayed Coker
`120
`0.0
`Fluid Coker
`201
`0.0
`Flex Coker
`37
`68.0 3.4
`Thermal Cracker
`27
`260.1
`99.1
`Visbreaker
`31.3
`SDA
`27
`36.6
`206.6 145.0
`50
`CCR
`26
`741.8 358.9
`PTA
`17.5
`0.0
`C41som
`25
`28.0
`32.5
`60.5
`C5/C61som
`16.8 2.0
`55
`18.8
`C3 Poly
`55
`26.5
`19.3
`45.8
`HFAiky
`55
`29.8 12.9
`42.7
`H2S04Aiky
`65
`348.9
`280.6
`629.5
`Resid Hds
`25
`1625.3
`768.1
`2393.4
`DistHds
`739.6
`40
`195.4
`935.0
`FCC Fd Hdt
`8.7
`10
`0.0
`MTBE
`8.7
`45
`1752.4
`1208.9
`543.5
`Naphtha Hds
`390.8 50
`Hydrogen Pit, MMSCF 1581.8 1191.0
`20
`Sulfur Pit, LT/D
`3283.0 4269.0
`7552.0
`
`71.4
`359.2
`67.9
`351.6
`1100.7
`
`Total Onsite
`Offsite Factor (Retrofit)
`Offsite Factor (Grass Roots)
`Grass Roots Share
`
`
`Weighted Offsite Factor
`$MM
`
`Area Factor
`
`Tot. Region Invest. $MM
`
`OnSite + Offsite,
`MBD *
`
`Region MJDN Production,
`
`$ Invest/Daily Bbl MJDN
`ROI Factor
`
`Capital Charge
`
`$/BBI MJDN
`¢/Gal MJDN
`
`* FC-1 reference
`
`
`
`case hydrocarbon MJDN volumes
`
`
`
`02-Jun-93 Revised
`
`APP L.Vll.6-9
`
`150
`44
`20
`70
`70
`30
`30
`25
`25
`25
`25
`25
`25
`35
`20
`10
`15
`19
`19
`19
`35
`30
`35
`2
`35
`60
`222
`
`0.33
`633.9
`311.5
`0.57
`0.81
`92.3
`2.14
`864.2
`353.6
`3.93
`606.1
`3.67
`0.0
`4.83
`252.1
`4.40
`0.0
`4.80
`0.0
`8.04
`5.0
`1.48
`107.0
`1.08
`39.5
`1.08
`207.1
`1.43
`466.6
`1.30
`0.0
`1.75
`54.2
`1.67
`5.8
`2.89
`55.9
`2.89
`37.3
`2.89
`521.1
`1.86
`640.1
`0.83
`223.3
`1.14
`43.5
`5.00
`698.8
`1.29
`325.7
`0.83
`0.09 384.6
`
`6929.3
`0.65
`1.0
`0.2
`0.72
`11918.4
`
`1.0
`11918.4
`
`7246.0
`4.51
`0.24
`
`1.08
`2.58
`
`FORD Ex. 1143, page 634
` IPR2020-00013
`
`

`

`Table APP.L.VII.6-8
`
`US Refining Industry
`
`
`Increase in Process Unit Capacity
`
`1995-1989 Reference Cases
`PADD I PADD II PADD Ill PADD IV PADD V PADD V TOTAL
`
`CA exCA LS
`9 1 1,12 10, 13
`
`All
`
`NPC Regions 1,2, 3, 4 5,6,7
`Capacity
`Unit
`Atm. Crude MBPD
`Vac. Crude MBPD
`
`8
`
`0 5 5 166 1 4 0 6 4 2 98
`3 3 0
`87
`8
`0 4 6 0
`
`FCnJ
`
`MBPD
`ResidFCCU MBPD
`Hydrocracker MBPD
`
`Resid Hydrocrack1 MBPD
`Delayed Coker MBPD
`Fluid Coker MBPD
`Flexicoker MBPD
`Visbreaker MBPD
`
`Solv. Deasphalter MBPD
`CC Reformer MBPD
`LP SR Reformer MBPD
`MBPD
`C41som
`C5/C6 lsom MBPD
`MBPD
`C3= Poly
`HF Alkylation MBPD
`H2S04 Alkylation MBPD
`MBPD
`ResidHDS
`
`Distillate HDS MBPD
`MBPD
`Added severity
`For CA LAD MBPD
`FCCUHDS MBPD
`Naphtha HDS MBPD
`MBPD
`MTBE
`LTD
`Sulfur
`
`Hydrogen Plant MMSCFD
`
`9 6 9 138 5 33
`9 2 63
`0
`0
`0
`0
`0
`0
`0
`1 2 3 7 1 13
`3 7 8
`2
`0
`0
`0
`0
`0
`0
`0
`2 6 0 0 148
`4 82
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`1 6
`0
`0
`4 12
`0
`5
`0
`9 1 95
`0 1 8 2 0
`2 3
`0
`0
`0
`0 2 3 0
`4 1
`2
`0
`0
`3 3 6
`0
`9 0
`1 8 1 1 5 2 0
`9
`0
`0
`0
`0
`0
`0
`0
`0
`3 2
`0
`1
`1
`3 2 8
`0
`4 8
`0 1 7 2
`6 14
`10
`18
`0
`0
`0
`0 18
`0
`0 3 10 265 1 9 5 1 1 00 7 4 4
`9 1 6 1 1 232
`3 2 6 3 9 9
`138
`1 38
`1 5 7 5 0
`9 0
`0
`0
`0
`6 4
`7
`0
`3
`0 17 3 8
`1 16
`13 2 5 6 2 0 1 4 2
`1 5 3 5 5 7 94 83 1 04 9 6 1 ,4 4 7
`0 6 8 7 0 0 88 2 3 2 4 9
`
`MBPD = Thousand Barrels per Day
`
`
`
`MMSCFD = Million Standard Cubic Feet per Day
`LTD= Long Tons per Day
`
`APP L.VII.6-10
`
`FORD Ex. 1143, page 635
` IPR2020-00013
`
`

`

`Table APP.L.VII.6-9
`
`US Refining Industry
`Investment Cost of Process Unit Capacity Increases
`
`
`1 995-1989 Reference Cases
`PADD I PADD II PADD Ill PADD IV PADD V PADD V TOTAL
`
`CA exCA LS
`9 1 1,1 2 10, 13
`
`All
`
`NPC Regions 1,2, 3 ,4 5,6,7
`
`Process Unit Investment, million 1990 $
`0 1 7 5 3
`Atm. Crude
`0
`0 25
`Vac. Crude
`
`8
`
`FOOJ
`
`ResidFCCU
`Hydrocracker
`Resid Hydrocracker
`Delayed Coker
`Fluid Coker
`Flexicoker
`Visbreaker
`Solv. Deasphalter
`CC Reformer
`LP SR Reformer
`C41som
`C5/C6 lsom
`C3= Poly
`HF Alkylation
`H2S04 Alkylation
`ResidHDS
`Distillate H DS
`ForCA LAD
`FCCUHDS
`Naphtha HDS
`Mtbe
`
`1 9 142 285 9 6 8 1 9 541
`
`4
`4
`
`9 5
`0 20
`2 1 6 4 8
`
`0
`0
`0
`0
`0
`0
`0
`4 79 23 398
`9 275
`7
`0
`0
`0
`0
`0
`0
`0
`0 1 5 346 1 0 253 0 6 24
`1
`0
`0
`0
`0
`0
`1
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`0
`1 6
`0
`4 1 2 0
`0
`0
`0 1 2 268
`0
`7
`0 249
`28
`0
`0
`0
`0
`0 28
`5 6 1 3
`0
`6 8
`0
`0
`1 45
`29 1 8 84
`0 1 4 0
`0
`1
`0
`0
`1
`0
`0
`8 79
`89
`2
`0
`0
`1
`26 1 7 38
`0 4 7
`5 1 34
`0 3 2
`3 2
`0
`0
`0
`0
`26 298 291 23 5 4 89 781
`0
`0 302 0 296
`0
`0
`1 6 82
`0
`0
`9 8
`0
`0
`0 2 1 4 7
`3
`0
`79
`9
`6 3 1 18 296 2 6 9 9
`5 5 8
`
`Sulfur
`
`1 3 1 6 9 7
`
`9
`
`8
`
`1 25
`
`Hydrogen Plant
`
`0 5 4 5 6 0 71 1 9 200
`
`TOTAL PROCESS UNITS
`
`1 73 1 ,0 58 2,023 9 5 1 ,049 231 4 , 6 25
`
`% Addon for offsite
`
`etc
`
`AREA FACTOR
`
`6 5 6 5 6 5 6 5 85 6 5
`1 .2 1 .2
`1 1 .2 1 .2 1 .2
`
`TOTAL PRCUECTINVESTMENT 343 2,096 3,339 1 8 8 2,330 4 5 8 8,752
`
`APP L.VII.6-11
`
`FORD Ex. 1143, page 636
` IPR2020-00013
`
`

`

`TABLE APP.L.VII.6-10
`
`U.S. REFINING INDUSTRY
`INVESTMENT CO ST O F PROCESS UNIT CAPACITY INCREASES
`1 995·1989 REFERENCE CASES
`
`PADDI PADD II PADD Ill PADDIV PADDV
`CA
`1 1, 1 2
`
`8
`
`9
`
`PADDV
`ex CA
`1 0, 1 3
`
`1 , 2, 3, 4 5,6, 7
`
`NPC Regions
`Process Invest-
`ment,