Single Octane NCG

Exhibit A-1: Estimated Aggregate Petroleum Refining Capacity, 2007

(K b/calendar day, except as noted)

Type of PADD PADD 4 & 5 Total

Process Process 1 2 3 ex Calif. California U.S.

Crude Distillation Atmospheric 1,589 3,640 8,440 1,860 1,918 17,447

Vacuum 638 1,457 3,890 655 1,115 7,756

Conversion Coking

 Delayed 44 363 1,192 136 349 2,085

 Fluid 47 16 86 20 98 266

 Other 39 22 61

Fluid Cat Cracking 692 1,187 2,943 354 682 5,858

Hydrocracking

 Distillate 225 618 131 362 1,336

 Resid 39 122 160

 Lube 51 38 89

 Other 33 65 98

Visbreaking 12 10 22

Thermal Cracking 10 10

Upgrading Alkylation 97 246 581 78 176 1,177

 Sulfuric 51 84 293 43 138 608

 Hydrofluoric 46 162 288 35 38 569

Pen/Hex Isomerization 17 173 235 43 111 580

Reforming 294 851 1,756 314 421 3,635

 Low Pressure 92 286 718 84 1,179

 All Other 203 564 1,038 314 337 2,456

Polymerization 18 5 22 10 4 59

Dimersol 3 8 1 5 17

Ether Production MTBE 3 28 3 34

TAME 3 3

Hydrotreating Naphtha Feed 348 1,080 2,309 362 461 4,560

Naphtha/Aromatics Sat. 10 11 23 64 108

FCC Naphtha 321 335 1,095 81 119 1,951

Kerosene & Distillate 479 1,020 2,241 354 442 4,536

Distillate/Aromatics Sat. 18 85 45 148

FCC Feed/Heavy Gas Oil 44 542 1,400 99 598 2,683

Resid 10 244 254

Lube Oil 1 24 75 39 139

Other 16 3 224 11 65 319

Other BTX Plant 41 50 283 1 375

Other Aromatics 12 8 46 66

Butane Isomerization 38 24 107 26 47 242

Hydrogen (MM scf/d)

 Production 84 634 1,024 265 1,183 3,190

 Recovery 31 178 684 119 120 1,132

Lube Oil 19 17 144 20 199

Solvent Deasphalting 20 16 200 35 59 330

Coke (K t/d) 5 19 70 6 19 119

Sulfur Recovery (K Sh t/d) 1.3 4.7 19.1 1.3 3.8 30

Asphalt 28 256 126 67 43 520

Complexity 9.0 9.5 10.7 6.9 13.2 10.2

1 Includes production and recovery.

Sources: Capacity derived from "2007 Worldwide Refinery Survey," Oil & Gas Journal , Dec. 18, 2007;

 DOE 2007 Refinery Capacity Survey (DOE website); and Petrolum Supply Annual , 2007, EIA/DOE.

 Generalized Complexity Index Scores: Oil & Gas Journal , March 18, 1996, p. 74-80.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-2:

Product/Source

Gasoline

Refinery & Blender Production2

 Net Blendstock Purchases

 Net Imports

 Net Inter-PADD

 Net Adjustments

 Production - Blndstk Purch3

Net Imports

Net Inter-PADD Shipments

Shipments from Puget Sound

Shipments from CA

RFG

Refinery & Blender Production2

 Net Blendstock Purchases

 Net Imports

 Net Inter-PADD

 Net Adjustments

 Production - Blndstk Purch3

Net Imports

Net Inter-PADD Shipments

Shipments from Puget Sound

Shipments from CA

CG

Refinery & Blender Production2

 Net Blendstock Purchases

 Net Imports

 Net Inter-PADD

 Net Adjustments

 Production - Blndstk Purch

Net Imports

Net Inter-PADD Shipments

Shipments from Puget Sound

Shipments from CA

Jet Fuel & Kerosene

Refinery Production

Net Imports

Net Inter-PADD Shipments

Net shipments from CA

Distillate Fuel Oil

Refinery Production

Net Imports

Net Inter-PADD Shipments

Net shipments from CA

Residual Oil

Refinery Production

Net Imports

Net Inter-PADD Shipments

Net shipments within P4&5

Other Products

Petrochemical Fdstk.

Refinery Production

Net Imports

Net Inter-PADD Shipments

Lubes & Waxes

Refinery Production

Net Imports

Net Inter-PADD Shipments

Asphalt & Road Oil

Refinery Production

Net Imports

Net Inter-PADD Shipments

Average Daily Supply of Major Refined Products, by Region

(K b/d)

2007

PADD PDs 4&5 U.S.

12345 ex Calif1 Calif. Total

3,331 2,614 1,412 293 1,625 901 1,017 9,275

1,763 2,103 3,345 288 1,490 692 1,086 8,989

879 200 -374 2 109 42 69 816

625 -1 51 63 1 62 738

239 154 -431 38 31 7

15 47 6 2 8 78

823 1,892 3,759 286 1,378 647 1,017 8,138

332 -8 -69 30 2 28 285

1,236 519 -1,864 5 105 110 1

-57 57

175 -175

1,275 412 318 1,087 70 1,017 3,092

1,276 412 367 1,053 68 985 3,108

551 100 -356 43 31 12 338

309 3 7 0 7 319

229 97 -362 36 31 5

13 3 3 19

664 301 763 1,007 34 973 2,735

-1 -14 -1 -1 -16

-35 35 35

-57 57

46 -46

2,056 2,202 1,094 293 538 831 0 6,183

487 1,691 2,978 288 437 624 101 5,881

328 100 -18 2 66 11 57 478

316 -1 48 56 1 55 419

10 57 -69 2 0 2

2 44 3 2 8 59

159 1,591 2,996 286 371 613 44 5,403

333 -8 -55 31 2 29 301

1,236 519 -1,829 5 70 75 1

130 -130

644 310 133 56 509 303 262 1,654

92 202 756 31 403 200 234 1,484

93 -7 -17 100 16 84 170

459 115 -606 25 6 31

55 -55

1,351 1,264 802 182 569 472 279 4,170

495 928 2,012 159 539 350 348 4,133

192 -166 8 1 -17 26 37

664 336 -1,044 15 29 43 1

95 -95

334 42 170 14 156 60 110 715

121 55 319 14 164 108 70 673

172 -3 -118 -8 -37 29 42

41 -10 -31

-11 11

27 48 559 1 9 3 7 643

18 39 334 1 7 2 6 399

5 5 233 2 1 1 244

4 4 -8

31 31 72 14 -3 17 147

18 17 141 17 0 17 191

-3 -3 -37 -2 -2 -44

16 17 -32 -1 -1

131 174 73 51 47 59 39 477

84 175 102 48 46 55 39 456

23 -6 3 1 4 21

24 -1 -23

Note: Increases in stocks are included in total product supplied and vice versa.

1 Includes refined products supplied by California refineries.

2 Includes "adjustments" reported by EIA for gasoline.

3 Adjusted for 10% ethanol blending with purchased blendstocks (5.7% in PADD 5).

Source: Derived from Tables 2, 4, 6, 8, 10, 12 & 26, Petroleum Supply Annuals, DOE/EIA.; CEC Refinery Reports;

 Prime Supplier Sales, EIA Website; Table M-21, FHWA; and Company-Level Import Data, DOE.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-3:

Net Inputs

Crude Oil

Natural Gas Liquids and LPG

 Pentanes Plus

 Liquified Petroleum Gases

 Normal Butane-Butylene

 Isobutane-Isobutylene

Other Liquids

Other Hydrocarbons/Oxygenates

 Other Hydrocarbons-Hydrogen

 Oxygenates2

 Fuel Ethanol

 MTBE

 Other

Unfinished Oils

 Naphtha and Lighter

 Kerosene and Light Oils

 Heavy Gas Oils

 Residuum

Gasoline Blending Components

Av-Gas Components

Process Feeds (K b/d)

Catalytic Cracking

Catalytic Hydrocracking

Delayed and Fluid Coking

Crude Oil Qualities

API Gravity (degrees)

Specific Gravity

Sulfur Content (wtg avg %)

Annual Refinery Net Inputs and Outputs, by Region

(K b/d)

2007

PADD 1 PADD 2 PADD 3 P45 ex CA CA US

1,745 3,456 8,138 1,394 1,944 16,640

1,513 3,226 7,315 1,361 1,741 15,156

16 92 247 55 8 419

49 98 3 21 171

16 43 150 52 -14 248

5 0 44 22 -14 58

12 43 106 30 190

215 137 575 -22 196 1,064

46 77 142 28 79 372

0 16 63 14 21 114

45 61 80 14 58 257

45 61 80 14 58 257

0 0

170 60 433 -42 72 693

32 19 25 -3 -16 57

-7 22 -33 -3 -12 -34

59 40 365 -31 94 526

86 -20 76 -5 7 145

-9 45

-1 0 0 -1

647 1,031 2,678 300 594 5,250

34 255 503 131 359 1,283

88 307 1,152 69 418 2,034

32.2 32.3 29.9 33.6 25.6 30.4

0.864 0.864 0.877 0.857 0.901 0.874

0.84 1.37 1.65 0.80 1.62 1.43

Note: Negative numbers indicate net production.

1 Estimated

2 Corresponds to RBOB, CBOB, and finished oxygenated gasoline production.

Sources: Derived from (1) refinery input data from EIA Website; and

 (2) CEC Refinery Reports, 2005 - 2008.

October 8, 2010 Page 1 of 2 MathPro
Single Octane NCG

Exhibit A-3:

Net Outputs

Liquified Petroleum Gases

Ethane-Ethylene

 Ethane

 Ethylene

Propane/Propylene

 Propane

 Propylene

Normal Butane/Butylene

Isobutane/Isobutylene

Finished Refined Products1

Finished Gasoline Outputs2

 Reformulated Motor Gasoline

 with Ether

 with Alcohol

 Non-Oxygenated

 Conventional Motor Gasoline

 with Alcohol

 Other

Aviation Gasoline

Kerosene-Type Jet Fuel

Kerosene

Distillate

 0-15 ppm Sulfur

 15-500 ppm Sulfur

 > 500 ppm Sulfur

 CARB Diesel

Residual Fuel Oil

 0-0.3 Sulfur

 0.31-1.0 Sulfur

 Greater Than 1% Sulfur

Pet Chem Feedstocks

 Naphtha

 Other Oils

Special Naphtha

Lubes

Waxes

Petroleum Coke

 Marketable

 Catalyst

Asphalt and Road Oil

Still Gas

Miscellaneous

 Fuel Use

 Nonfuel Use

Processing Gain

Annual Refinery Net Inputs and Outputs, by Region

(K b/d)

2007

PADD 1 PADD 2 PADD 3 P45 ex CA CA US

1,712 3,369 7,884 1,340 1,851 16,119

52 107 363 22 39 582

0 0 20 20

14 14

006 6

52 107 343 22 39 562

33 83 163 19 33 330

19 23 180 2 7 232

000 0

000 0

1,660 3,263 7,521 1,318 1,811 15,537

829 1,828 3,769 600 1,086 8,076

453 307 760 47 960 2,528

0 0

453 307 751 47 942 2,500

9 0 18 27

376 1,521 3,009 553 126 5,549

302 47 114 36 498

376 1,219 2,962 439 90 5,050

3 11 2 16

84 200 731 199 234 1,448

8 2 25 1 36

495 927 2,013 351 348 4,133

267 785 1,212 496 81 2,841

34 94 462 38 15 642

194 49 338 64 5 650

0 0 0 -247 247 0

121 55 319 108 70 673

40 0 32 6 3 81

55 5 25 31 20 136

25 51 262 71 46 455

18 39 334 1 6 399

18 31 151 0 0 200

8 183 1 6 199

1 5 35 1 42

17 14 132 0 17 179

1 3 9 0 12

53 140 462 39 129 823

20 97 345 23 99 584

33 43 117 16 31 239

84 175 102 55 39 456

65 137 334 - - 697

3 12 40 0 12 68

0001

3 12 40 0 12 68

-85 -190 -538 -183 -996

1 Excludes petroleum coke, still gas, and miscellaneous fuel use

2 Includes RBOB and CBOB volumes and associated oxygenate volumes.

Sources: Derived from (1) refinery output data from EIA Website; and

 (2) CEC Refinery Reports, 2005 - 2008.

October 8, 2010 Page 2 of 2 MathPro
Single Octane NCG

Exhibit A-4:

Product Description

Net InputsCrude OilPentanes PlusIso-butaneNormal ButaneOxygenates

 MTBE (max) Fuel Ethanol for RFG Fuel Ethanol for CG

Gasoline Blending ComponentsUnfinished Oils

 Naphtha & Lighter Kerosene & Light Gas Oils Heavy Gas Oils Residuum

Process Feeds (K b/d)Catalytic CrackingCatalytic HydrocrackingDelayed and Fluid CokingCrude Oil QualitiesAPI Gravity (degrees)Specific GravitySulfur Content (wtg avg %)

Seasonal Refinery Net Inputs and Outputs, by Region(K b/d)

2007

PADD 1 PADD 2 PADD 3 PADD 45 ex CA CA 

Summer Winter Summer Winter Summer Winter Summer Winter Summer Winter 

1,796 1,751 3,489 3,409 8,119 8,051 1,482 1,460 1,910 1,911,534 1,511 3,265 3,140 7,383 7,158 1,396 1,322 1,750 1,82

55 36 98 97 3 5 20 2

14 13 46 43 112 106 30 28 2 

26 67 116 40 1

46 45 60 68 78 85 107 111 

46 45 30 31 74 78 93 97 

0 30 36 4 7 10 11 4 

22 -11 -10 51 3

180 157 81 54 458 496 -47 -38 88 1

33 21 22 22 36 28 -4 -1 -11 -3

-8 -9 32 15 -36 12 -5 -14 -15 

56 72 46 40 393 385 -31 -24 107 898 73 -19 -22 65 71 -7 1 6 -3

653 653 1,062 960 2,670 2,662 200 267 607 53

33 32 258 254 514 509 134 134 368 3788 88 304 309 1,163 1,096 91 113 422 42

32.3 32.2 32.4 32.3 29.8 29.6 33.7 33.8 25.7 25.

0.864 0.864 0.863 0.864 0.877 0.878 0.857 0.856 0.900 0.90

0.87 0.83 1.35 1.39 1.65 1.69 0.79 0.78 1.59 1.6

October 8, 2010 Page 1 of 2 
Single Octane NCG

Exhibit A-4:

Product Description

Net Outputs1Liquified Petroleum GasesEthane-Ethylene

 Ethane Ethylene

Propane/Propylene

 Propane Propylene

Normal Butane-Butylene

 Normal Butane Normal Butylene

Isobutane-Isobutylene

 Isobutane Isobutylene

Finished Refined Products1Gasolines Reformulated

 with Ether with Alcohol Non-Oxygenated

 Conventional (incl. Eoh-blended) CARBOBAviation GasolineJet Fuel & KeroseneDistillate

 0-15 ppm Sulfur 15-500 ppm Sulfur > 500 ppm Sulfur

Residual Fuel Oil

 0-0.3 Sulfur 0.31-1.0 Sulfur Greater Than 1% Sulfur

Pet Chem Feedstocks

 Naphtha Other Oils

Special NaphthaLubes & WaxesPetroleum Coke

 Marketable Catalyst

Asphalt and Road OilMiscellaneous, Non-fuel use

Seasonal Refinery Net Inputs and Outputs, by Region(K b/d)

2007

PADD 1 PADD 2 PADD 3 PADD 45 ex CA CA 

Summer Winter Summer Winter Summer Winter Summer Winter Summer Winter 

1,752 1,722 3,415 3,330 7,870 7,860 1,326 1,309 1,844 1,85

72 53 172 103 399 353 17 23 68 3

0 0 0 0 19 19 

14 13 

000056 

51 51 106 103 342 344 20 23 40 3

32 31 82 85 166 156 19 20 24 18 176 188 

19 0 66 0 38 -10 -3 0 28 

19 63 40 

0 0 3 0 -3 -10 

2100 0 0 

2100 0 0 

1,679 1,669 3,243 3,227 7,471 7,507 1,309 1,286 1,776 1,81

837 848 1,819 1,825 3,751 3,826 589 603 1,051 1,03459 445 303 314 757 783 28 

459 445 303 314 738 783 

19 28 

378 403 1,516 1,511 2,994 3,042 551 547 154 7

39 57 869 96

3 3 12 11 2 2 

89 95 198 203 751 756 202 191 225 28

494 497 922 932 2,005 2,033 357 340 357 36

273 264 792 817 1,211 1,366 252 243 337 35

39 27 88 69 496 442 44 55 14 

182 207 42 46 298 225 60 43 5 

124 116 57 56 321 295 108 110 66 8

39 48 0 0 32 28 90 83 59 39 5 6 24 28 44 38 26 29 52 50 265 240 67 71 

20 18 40 37 338 326 3 1 5 

20 18 31 29 154 141 1 1 

9 8 184 185 4 1 

1 0 4 3 34 43 1 1 

18 17 16 15 144 136 0 0 18 153 57 140 141 467 452 40 38 132 12

20 23 96 100 353 335 23 22 100 933 35 44 41 114 117 17 15 32 2

97 76 182 153 114 80 59 49 42 2

0 -12 -12 13 1

1 Excludes petroleum coke, still gas., and miscellaneous fuel use.Sources: Refiney Net Inputs & Outputs, Downstream Feed Rates, and Crude Oil Qualities from EIA website and Monthly Refinery Repor

October 8, 2010 Page 2 of 2 
Single Octane NCG

Exhibit A-5: Distillation Curves and Whole Crude Properties for Regional Composite Crud

Fractions & PADD

Properties 1 2 3 Calif U.S.

Volume (K b/d) 1,541 3,297 7,260 1,798 15,242

CRUDE FRACTIONSLPGs: Ethane 0.001 0.001 0.001 0.001 0.001 Propane 0.004 0.003 0.004 0.003 0.003 Isobutane 0.003 0.003 0.003 0.003 0.003 Butane 0.010 0.010 0.009 0.010 0.010Naphthas: Very Light (C5-160) 0.045 0.047 0.046 0.032 0.045 Light (160-250) 0.069 0.081 0.071 0.059 0.073 Medium (250-325) 0.067 0.074 0.066 0.053 0.067 Heavy (325-375) 0.051 0.048 0.046 0.035 0.045Middle Distillates: Kerosene (375-500) 0.129 0.127 0.122 0.104 0.121 Distillate (500-620) 0.124 0.122 0.119 0.114 0.120Atmospheric Resid: Light gas oil (620-800) 0.162 0.162 0.158 0.167 0.161 Heavy gas oil (800-1050) 0.168 0.170 0.167 0.199 0.172 Resid (1050+) 0.098 0.063 0.055 0.088 0.070 Asphalt (1050+) 0.069 0.089 0.132 0.132 0.107Total: 1.000 1.000 1.000 1.000 1.000WHOLE CRUDEAPI Gravity 31.2 32.1 29.8 25.5 30.2Sulfur (wt %) 1.01% 1.35% 1.64% 1.50% 1.44%UtilitiesFuel (foeb/b) 0.015 0.015 0.014 0.014 0.014Steam (lb/b) 33.0 33.3 32.6 32.2 32.8Electricity (kWh/b) 0.85 0.85 0.85 0.88 0.85 0%

10%20%30%40%50%60%70%80%90%

100%

0 200 400 600 800 

Temperature (°F)

Percent Off

October 8, 2010 
Single Octane NCG

Exhibit A-6a: Reported Refinery Fuel Use, by PADD

MM btu/

Region Type of Fuel fuel unit

U.S. Energy Use (Trillion btu)

Crude Oil (K bbl) 5.8

LPG's (K bbl) 3.8

Distillate (K bbl) 5.8

Residual Fuel (K bbl) 6.3

Still Gas (K foeb @ 6.0MM btu/foeb) 6.0

Marketable Petroleum Coke (K bbl) 6.02

Catalyst Petroleum Coke (K bbl) 6.02

Other Products (K bbl)1 5.25

Natural Gas (million cf) 1.1

Coal (K short tons) 21

Purchased Electricity (Million Kwh) 9.977

Purchased Steam (million lbs) 1.3

PADD 1 Energy Use (Trillion btu)

Crude Oil (K bbl) 5.8

LPG's (K bbl) 3.8

Distillate (K bbl) 5.8

Residual Fuel (K bbl) 6.3

Still Gas (K foeb @ 6.0MM btu/foeb) 6

Marketable Petroleum Coke (K bbl) 6.02

Catalyst Petroleum Coke (K bbl) 6.02

Other Products (K bbl) 5.25

Natural Gas (million cf) 1.1

Coal (K short tons) 21

Purchased Electricity (Million Kwh) 9.977

Purchased Steam (million lbs) 1.3

PADD 2 Energy Use (Trillion btu)

Crude Oil (K bbl) 5.8

LPG's (K bbl) 3.8

Distillate (K bbl) 5.8

Residual Fuel (K bbl) 6.3

Still Gas (K foeb @ 6.0MM btu/foeb) 6

Marketable Petroleum Coke (K bbl) 6.02

Catalyst Petroleum Coke (K bbl) 6.02

Other Products (K bbl) 5.25

Natural Gas (million cf) 1.1

Coal (K short tons) 21

Purchased Electricity (Million Kwh) 9.977

Purchased Steam (million lbs) 1.3

PADD 3 Energy Use (Trillion btu)

Crude Oil (K bbl) 5.8

LPG's (K bbl) 3.8

Distillate (K bbl) 5.8

Residual Fuel (K bbl) 6.3

Still Gas (K foeb @ 6.0MM btu/foeb) 6

Marketable Petroleum Coke (K bbl) 6.02

Catalyst Petroleum Coke (K bbl) 6.02

Other Products (K bbl) 5.25

Natural Gas (million cf) 1.1

Coal (K short tons) 21

Purchased Electricity (Million Kwh) 9.977

Purchased Steam (million lbs) 1.3

2005 2006 2007 2008

3,231 3,352 3,338 3,295

0000

4,175 2,656 2,663 2,930

755 434 420 472

2,207 2,018 1,844 1,390

238,236 249,358 247,106 237,161

2,242 458 648 364

87,410 90,034 87,367 81,447

5,329 6,327 3,704 3,840

682,919 697,593 667,986 710,500

41 34 39 43

36,594 39,353 41,829 42,682

63,591 70,769 99,022 98,769

305 285 295 284

0000

722 329 185 52

366 23 22 29

1,146 920 826 399

22,317 21,232 22,890 21,328

1,067 0 0 0

11,745 11,033 11,973 12,198

141 54 21 29

35,603 36,225 28,709 27,872

33 31 32 31

3,520 3,576 3,984 4,192

4,912 5,716 5,784 5,204

641 651 649 663

0000

779 567 842 804

50 45 47 44

163 206 189 194

50,213 49,585 49,429 48,882

0000

17,342 16,502 15,701 15,005

1,686 1,961 395 18

106,480 114,721 120,047 138,894

8 3 7 12

9,875 10,488 10,555 10,804

5,033 7,298 10,738 11,022

1,575 1,708 1,678 1,643

0000

359 277 208 516

86 111 115 107

4133

111,798 125,046 120,930 114,447

29 194 58 27

41,270 45,395 42,690 39,346

1,300 1,971 1,510 1,698

395,980 395,627 363,004 381,022

0000

16,620 18,612 20,433 20,675

34,738 38,999 63,471 63,756

October 8, 2010 Page 1 of 2 MathPro
Single Octane NCG

Exhibit A-6a: Reported Refinery Fuel Use, by PADD

MM btu/

Region Type of Fuel fuel unit

PADD 4 Energy Use (Trillion btu)

Crude Oil (K bbl) 5.8

LPG's (K bbl) 3.8

Distillate (K bbl) 5.8

Residual Fuel (K bbl) 6.3

Still Gas (K foeb @ 6.0MM btu/foeb) 6

Marketable Petroleum Coke (K bbl) 6.02

Catalyst Petroleum Coke (K bbl) 6.02

Other Products (K bbl) 5.25

Natural Gas (million cf) 1.1

Coal (K short tons) 21

Purchased Electricity (Million Kwh) 9.977

Purchased Steam (million lbs) 1.3

PADD 5 Energy Use (Trillion btu)

Crude Oil (K bbl) 5.8

LPG's (K bbl) 3.8

Distillate (K bbl) 5.8

Residual Fuel (K bbl) 6.3

Still Gas (K foeb @ 6.0MM btu/foeb) 6

Marketable Petroleum Coke (K bbl) 6.02

Catalyst Petroleum Coke (K bbl) 6.02

Other Products (K bbl) 5.25

Natural Gas (million cf) 1.1

Coal (K short tons) 21

Purchased Electricity (Million Kwh) 9.977

Purchased Steam (million lbs) 1.3

California Energy Use (Trillion btu)

Crude Oil (K bbl) 5.8

LPG's (K bbl) 3.8

Distillate (K bbl) 5.8

Residual Fuel (K bbl) 6.3

Still Gas (K foeb @ 6.0MM btu/foeb) 6

Marketable Petroleum Coke (K bbl)2 6.02

Catalyst Petroleum Coke (K bbl) 6.02

Other Products (K bbl) 5.25

Natural Gas (million cf)2 1.1

Coal (K short tons) 21

Purchased Electricity (Million Kwh) 9.977

Purchased Steam (million lbs) 1.3

Note: Electricity conversion factor represents btu's in delivered power adjusted for generatio

1 Gross heat of combustion of 5.25 MM btu/b taken from CEC data.

2 The volumes of marketable coke and natural gas used for energy by California refineries

 are larger than the corresponding volumes reported by EIA for all of PADD 5. The abov

 estimates, calculated as 80% of the numbers reported by EIA for PADD 5.

 estimates, calculated as 80% of PADD 5's reported energy use.

Source: Derived from EIA Website and from data provided by CEC.

2005 2006 2007 2008

111 115 113 118

0000

24 15 13 49

0000

167 121 83 49

8,208 8,496 8,304 9,121

176 154 473 234

2,652 2,664 2,599 2,641

502 142 62 68

21,585 24,830 22,513 22,762

0000

1,601 1,704 1,744 1,886

952 757 1,191 1,010

599 593 602 586

0000

2,291 1,468 1,415 1,509

253 255 236 292

727 770 743 745

45,700 44,999 45,553 43,383

970 110 117 103

14,401 14,440 14,404 12,257

1,700 2,199 1,716 2,027

123,271 126,190 133,713 139,950

0000

4,978 4,973 5,113 5,125

17,956 17,999 17,838 17,777

483 474 484 468

0 0 0 0

1,706 1,015 978 1,043

155 78 72 90

0 0 0 0

40,795 39,824 40,314 38,394

776 88 94 82

11,675 11,704 11,675 9,935

4 6 5 6

98,617 100,952 106,970 111,960

0 0 0 0

3,096 3,244 3,335 3,343

12,508 12,712 12,598 12,555

ion efficiency and transmission loss.

s, as reported by CEC,

ve numbers are

October 8, 2010 Page 2 of 2 MathPro
Single Octane NCG

Exhibit A-6b: Estimated Refinery Fuel Use, by PADD

Region Type of Fuel 2005 2006 2007 2008

U.S. Energy Use (Billion btu/d) 8,830 9,138 9,111 8,992

Natural Gas (K foeb/d)1 304 317 316 334

Still Gas (K foeb/d)2 629 655 649 624

Catalyst Coke (K b/d) 239 247 239 223

Power (MM Kwh/d)3 152 154 160 162

PADD 1 Energy Use (Billion btu/d) 825 784 810 780

Natural Gas (K foeb/d) 21 19 13 11

Still Gas (K foeb/d) 59 56 60 56

Catalyst Coke (K b/d) 32 30 33 33

Power (MM Kwh/d) 12 13 15 16

PADD 2 Energy Use (Billion btu/d) 1,763 1,791 1,781 1,820

Natural Gas (K foeb/d) 56 62 63 71

Still Gas (K foeb/d) 132 130 130 129

Catalyst Coke (K b/d) 48 45 43 41

Power (MM Kwh/d) 29 31 31 31

PADD 3 Energy Use (Billion btu/d) 4,355 4,691 4,627 4,533

Natural Gas (K foeb/d) 166 176 177 187

Still Gas (K foeb/d) 292 327 316 299

Catalyst Coke (K b/d) 113 124 117 108

Power (MM Kwh/d) 79 78 82 82

PADD 4 Energy Use (Billion btu/d) 305 311 310 324

Natural Gas (K foeb/d) 13 13 13 12

Still Gas (K foeb/d) 21 22 22 24

Catalyst Coke (K b/d) 7777

Power (MM Kwh/d) 4555

PADD 5 Energy Use (Billion btu/d) 1,577 1,561 1,581 1,536

Natural Gas (K foeb/d) 47 47 49 53

Still Gas (K foeb/d) 123 120 121 116

Catalyst Coke (K b/d) 39 40 39 34

Power (MM Kwh/d) 27 27 27 27

California Energy Use (Billion btu/d) 1,251 1,230 1,252 1,208

Natural Gas (K foeb/d) 25 25 27 30

Still Gas (K foeb/d) 109 106 107 102

Catalyst Coke (K b/d) 32 32 32 27

Power (MM Kwh/d) 21 21 21 21

Notes: Foeb defined as 6.3 million btu/b.

1 Calculated as the sum of energy (in foebs) from: (1) natural gas; (2) the minor categories of distillate, resid, marketable

 coke, other products, and coal; and (3) estimated natural gas used as fuel for purchased steam and hydrogen;

 less estimated natural gas used for refinery-based power generation.

2 Includes energy (in foebs) from LPGs and still gas.

3 Includes: (1) purchased power; (2) internally generated power not sold to the grid; and (3) estimated power used

 to produce purchased steam and hydrogen.

Source: Derived from: Annual Source and Disposition of Electricity for Non-Utility Generators, 2006 & 2007,

 EIA Website (EIA 906 & 920 Surveys); ARMS Modeling results for hydrogen production; and Exhibit A-6a.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-7a: Estimated Refinery Energy Use, by PADD

Refinery Inputs, Outputs Average

Region & Energy Use 2005 2006 2007 2008 2005-2008

U.S. Refnery Inputs (K b/d)1 15,725 15,841 15,827 15,364 15,689

Refnery Outputs (K b/d)2 15,266 15,367 15,416 15,021 15,267

Energy Use (Billion btu/d) 8,830 9,138 9,111 8,992 9,018

 Fuel 7,314 7,606 7,518 7,377 7,454

 Power3 1,516 1,532 1,592 1,615 1,564

PADD 1 Refnery Inputs (K b/d)1 1,710 1,630 1,659 1,593 1,648

Refnery Outputs (K b/d)2 1,682 1,602 1,626 1,572 1,621

Energy Use (Billion btu/d) 825 784 810 780 800

 Fuel 702 654 658 622 659

 Power3 123 130 153 158 141

PADD 2 Refnery Inputs (K b/d)1 3,309 3,312 3,246 3,253 3,280

Refnery Outputs (K b/d)2 3,222 3,236 3,176 3,185 3,205

Energy Use (Billion btu/d) 1,763 1,791 1,781 1,820 1,789

 Fuel 1,471 1,482 1,476 1,507 1,484

 Power3 292 310 306 313 305

PADD 3 Refnery Inputs (K b/d)1 7,441 7,655 7,755 7,343 7,549

Refnery Outputs (K b/d)2 7,215 7,400 7,560 7,180 7,339

Energy Use (Billion btu/d) 4,355 4,691 4,627 4,533 4,552

 Fuel 3,569 3,915 3,812 3,711 3,751

 Power3 787 777 816 822 800

PADD 4 Refnery Inputs (K b/d)1 562 556 546 540 551

Refnery Outputs (K b/d)2 543 537 525 520 531

Energy Use (Billion btu/d) 305 311 310 324 313

 Fuel 261 264 263 272 265

 Power3 44 47 48 52 48

PADD 5 Refnery Inputs (K b/d)1 2,702 2,688 2,621 2,634 2,661

Refnery Outputs (K b/d)2 2,605 2,591 2,528 2,564 2,572

Energy Use (Billion btu/d) 1,577 1,561 1,581 1,536 1,564

 Fuel 1,307 1,292 1,311 1,265 1,294

 Power3 270 269 271 271 270

California Refnery Inputs (K b/d)1 1,928 1,904 1,841 1,866 1,885

Refnery Outputs (K b/d)2 1,856 1,832 1,769 1,794 1,813

Energy Use (Billion btu/d) 1,251 1,230 1,252 1,208 1,235

 Fuel 1,041 1,016 1,039 994 1,022

 Power3 210 214 214 214 213

Note: Excludes energy to produce power for sale to grid; iincludes estimated energy to produce purchased hydrogen.

1 Calculated as the sum of crude oil, heavy gas oils, and residuum imputs.

2 Calculated as the sum of liquified petroleum gases, finished refined products (excluding catalyst coke,still gas,

 & and miscellaneous fuel use), and output of gasoline and av-gas blending components (from refinery input table),

 less the sum of inputs of natural gas liquids, other hydrocarbons/oxygenates, naphtha and lighter materials, and

 kerosene & light oils.

3 Represents btu's in delivered power, adjusted for generation efficiency and transmission loss.

Source: Derived from Exhibit A-3 and A-6b.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-7b: Average Per Barrel Refinery Energy Use, by PADD

(Million btu per Barrel)

Average

Region Refinery Energy Use 2005 2006 2007 2008 2005-2008

U.S. Per Refinery Input 0.56 0.58 0.58 0.59 0.57

 Fuel 0.47 0.48 0.48 0.48 0.48

 Power3 0.10 0.10 0.10 0.11 0.10

Per Refinery Output 0.58 0.59 0.59 0.60 0.59

 Fuel 0.48 0.49 0.49 0.49 0.49

 Power3 0.10 0.10 0.10 0.11 0.10

PADD 1 Per Refinery Input 0.48 0.48 0.49 0.49 0.49

 Fuel 0.41 0.40 0.40 0.39 0.40

 Power3 0.07 0.08 0.09 0.10 0.09

Per Refinery Output 0.49 0.49 0.50 0.50 0.49

 Fuel 0.42 0.41 0.40 0.40 0.41

 Power3 0.07 0.08 0.09 0.10 0.09

PADD 2 Per Refinery Input 0.53 0.54 0.55 0.56 0.55

 Fuel 0.44 0.45 0.45 0.46 0.45

 Power3 0.09 0.09 0.09 0.10 0.09

Per Refinery Output 0.55 0.55 0.56 0.57 0.56

 Fuel 0.46 0.46 0.46 0.47 0.46

 Power3 0.09 0.10 0.10 0.10 0.10

PADD 3 Per Refinery Input 0.59 0.61 0.60 0.62 0.60

 Fuel 0.48 0.51 0.49 0.51 0.50

 Power3 0.11 0.10 0.11 0.11 0.11

Per Refinery Output 0.60 0.63 0.61 0.63 0.62

 Fuel 0.49 0.53 0.50 0.52 0.51

 Power3 0.11 0.10 0.11 0.11 0.11

PADD 4 Per Refinery Input 0.54 0.56 0.57 0.60 0.57

 Fuel 0.46 0.47 0.48 0.50 0.48

 Power3 0.08 0.08 0.09 0.10 0.09

Per Refinery Output 0.56 0.58 0.59 0.62 0.59

 Fuel 0.48 0.49 0.50 0.52 0.50

 Power3 0.08 0.09 0.09 0.10 0.09

PADD 5 Per Refinery Input 0.58 0.58 0.60 0.58 0.59

 Fuel 0.48 0.48 0.50 0.48 0.49

 Power3 0.10 0.10 0.10 0.10 0.10

Per Refinery Output 0.61 0.60 0.63 0.60 0.61

 Fuel 0.50 0.50 0.52 0.49 0.50

 Power3 0.10 0.10 0.11 0.11 0.11

California Per Refinery Input 0.65 0.65 0.68 0.65 0.66

 Fuel 0.54 0.53 0.56 0.53 0.54

 Power3 0.11 0.11 0.12 0.11 0.11

Per Refinery Output 0.67 0.67 0.71 0.67 0.68

 Fuel 0.56 0.55 0.59 0.55 0.56

 Power3 0.11 0.12 0.12 0.12 0.12

Source: Derived from Exhibit A-7a.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-8: Reported Average Gasoline Properties, by Season,

Gasoline Type, and Producing-PADD2004

RFG CG Pool

PADD --> 1 2 3 4&51 123 4&51 123 4&

Summer (K b/d) 492 247 819 329 1,620 2,951 534 820 1,867 3,770 RVP (psi) 6.8 7.0 6.9 8.3 8.5 8.2 8.1 7.4 8.3 7.9 Oxygen (wt %) 2.7 3.5 2.3 0.5 0.3 0.2 1.8 0.7 0.6

 MTBE (vol %) 8.2 8.7 0.4 0.0 0.8 5.1 0.0 2.5 TAME (vol %) 0.0 0.6 0.0 0.0 0.0 0.0 0.0 0.1 ETBE (vol %) 0.0 0.0 0.0 Ethanol (vol %) 3.2 9.4 1.6 1.3 0.9 0.0 2.4 2.0 0.4

Aromatics (vol %) 21.0 18.9 18.7 28.5 28.4 27.3 29.1 24.0 27.2 25.4 Benzene (vol %) 0.51 0.84 0.55 0.91 1.37 0.97 1.72 0.67 1.30 0.87 Olefins (vol %) 13.7 5.3 11.4 13.2 8.7 12.1 10.2 13.5 8.3 12.0 Sulfur (pm) 99 78 73 127 139 108 114 110 131 100 E200 (% off) 47.0 46.6 48.8 43.7 46.6 44.6 44.8 45.7 46.6 45.5 E300 (% off) 82.2 84.7 82.4 80.4 81.4 79.4 83.3 81.5 81.8 80.0 API Gravity 57.6 58.8 58.7 57.3 58.3 58.1 58.3 57.5 58.4 58.2 Winter (K b/d) 524 295 729 335 1,592 2,763 586 858 1,887 3,492 RVP (psi) 13.0 13.3 11.8 13.2 13.2 11.9 12.6 13.1 13.2 11.9 Oxygen (wt %) 2.4 3.3 2.1 0.4 0.4 0.1 0.0 1.6 0.8 0.5 

 MTBE (vol %) 7.5 8.5 0.3 0.0 0.7 4.7 0.0 2.3 TAME (vol %) 0.0 0.7 0.0 0.0 0.0 0.0 0.0 0.2 ETBE (vol %) 0.0 0.0 0.0 0.0 0.0 Ethanol (vol %) 2.7 8.8 0.9 1.0 1.1 0.0 0.0 2.1 2.3 0.2 

Aromatics (vol %) 19.8 17.3 18.0 23.9 25.0 23.9 26.6 21.4 23.8 22.7 Benzene (vol %) 0.54 0.79 0.54 0.91 1.32 0.87 1.65 0.69 1.23 0.80 Olefins (vol %) 14.3 4.9 11.4 15.9 8.6 12.1 9.6 14.9 8.0 12.0 Sulfur (pm) 125 93 101 143 134 115 100 132 128 112 E200 (% off) 53.9 58.4 55.9 50.3 52.1 49.7 50.7 52.5 53.1 51.0 E300 (% off) 83.4 85.6 83.6 83.1 84.0 81.8 87.2 83.3 84.2 82.2 API Gravity 61.2 63.2 62.2 61.6 61.9 61.7 61.8 61.4 62.1 61.8 

1. Excludes California.Source: Derived from data provided by the U.S. Environmental Protection Agency.

October 8, 2010 
Single Octane NCG

Exhibit A-9: Average Properties of Gasoline Produced by U.S. Refineries (ex California), by Season and Gasoline Type

2000-2006

RFG CG 

2000 2001 2002 2003 2004 2005 2006 2000 2001 2002 2003 2004 2005 2006 2000 2001 200

Summer (K b/d) 1,748 1,734 1,744 1,756 1,846 1,732 1,591 5,308 5,378 5,630 6,034 6,014 5,629 5,975 7,056 7,111 7,3RVP (psi) 6.8 6.8 6.8 6.8 6.9 6.9 7.0 8.3 8.3 8.3 8.3 8.3 8.3 8.3 7.9 7.9 Oxygen (wt %) 2.2 2.2 2.3 2.3 2.6 2.5 3.5 0.7 0.6 0.7 0.8 1.0 1.0 0.0 1.1 1.0 

 MTBE (vol %) 9.0 8.9 8.7 8.7 7.3 6.8 0.1 1.6 1.7 1.7 2.1 2.0 1.6 0.0 3.4 3.5  TAME (vol %) 0.9 0.9 0.7 0.9 0.5 0.5 0.0 0.2 0.3 0.3 0.2 0.0 0.1 0.2 0.4 0.4  ETBE (vol %) 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0  Ethanol (vol %) 1.2 1.2 1.5 1.7 3.2 3.2 9.5 0.9 0.8 1.0 1.1 1.6 1.9 0.0 1.0 0.9 

Aromatics (vol %) 19.3 20.1 20.2 19.7 19.7 20.2 19.0 28.4 28.1 27.9 27.3 27.9 27.6 28.4 26.1 26.1 2Benzene (vol %) 0.59 0.62 0.58 0.60 0.59 0.65 0.58 1.15 1.17 1.10 1.13 1.15 1.23 1.25 1.01 1.04 0Olefins (vol %) 10.7 11.7 10.5 10.9 11.2 11.8 10.9 11.7 12.5 12.0 11.7 11.2 11.8 11.2 11.5 12.3 1Sulfur (pm) 126 129 129 114 81 74 39 322 308 300 306 119 108 58 273 264 2E200 (% off) 47.6 47.2 47.5 47.8 47.9 48.6 46.7 45.2 45.2 45.0 45.2 45.2 45.7 45.0 45.8 45.7 4E300 (% off) 84.5 84.2 84.2 84.3 83.3 84.0 84.2 80.6 81.0 80.5 80.7 80.6 81.6 81.9 81.6 81.8 8T50 (°F) 205 206 204 204 205 202 210 212 213 214 213 213 211 213 210 211 2T90 (°F) 328 327 329 329 335 331 333 336 334 336 336 335 331 330 334 332 3API Gravity 58.9 58.5 58.6 58.7 58.3 58.5 58.1 57.7 57.5 57.7 57.0 58.1 58.4 58.2 58.0 57.7 5Winter (K b/d) 1,781 1,733 1,783 1,822 1,869 1,887 1,893 5,707 5,766 5,814 5,678 5,617 5,542 5,370 7,488 7,499 7,5RVP (psi) - - - - - - - - - - - - - - - - Oxygen (wt %) 2.1 2.1 2.1 2.2 2.4 2.4 3.1 0.8 0.8 0.7 0.9 1.1 1.1 2.2 1.1 1.1 

 MTBE (vol %) 8.1 8.0 7.7 7.5 6.7 6.4 2.9 1.3 1.5 1.3 1.4 1.8 1.2 0.5 2.9 3.0  TAME (vol %) 0.7 0.7 0.6 0.4 0.4 0.3 0.1 0.2 0.2 0.2 0.1 0.1 0.1 0.0 0.3 0.3  ETBE (vol %) 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0  Ethanol (vol %) 1.3 1.3 1.5 1.8 2.9 3.0 6.8 1.2 1.3 1.3 1.6 2.2 2.5 6.1 1.3 1.3 

Aromatics (vol %) 19.0 19.2 19.4 19.3 18.9 19.3 19.2 24.7 25.1 24.8 24.4 24.5 24.4 24.4 23.3 23.7 2Benzene (vol %) 0.65 0.64 0.64 0.64 0.62 0.66 0.66 1.08 1.13 1.07 1.08 1.09 1.16 1.20 0.98 1.02 0Olefins (vol %) 12.0 12.3 11.0 11.0 11.2 11.1 10.7 11.9 12.3 11.6 11.2 11.2 11.3 11.0 11.9 12.3 1Sulfur (pm) 204 191 194 174 107 86 43 296 298 295 259 121 99 55 274 273 2E200 (% off) 56.2 55.9 56.3 56.1 56.1 56.3 56.4 50.4 49.9 50.2 50.4 50.8 50.8 51.0 51.8 51.3 5E300 (% off) 85.8 85.5 85.5 84.9 84.7 85.2 85.2 83.4 83.2 83.1 82.9 83.3 84.0 84.3 84.0 83.7 8T50 (°F) 183 184 182 182 181 180 173 199 202 202 200 199 200 200 195 198 1T90 (°F) 319 319 323 327 327 325 326 326 328 328 329 327 325 323 324 326 3API Gravity 62.4 62.1 62.2 62.1 62.0 61.9 61.5 61.5 60.8 61.0 60.5 61.8 61.9 62.1 61.7 61.1 6

Source: Derived from data provided by the U.S. Environmental Protection Agency.

October 8, 2010 
Single Octane NCG

Exhibit A-10a: Estimated Properties of Summer RFG, by PADD of Origin

Property 2000 2001 2002 2003 2004 2005 2006

PADD 1 Refineries1

RVP (psi) 6.8 6.8 6.8 6.8 6.9 6.9 6.9

Oxygen (wt%) 2.1 2.1 2.1 2.2 2.7 2.7 3.5

 MTBE (wt%) 10.5 10.9 10.7 10.9 6.5 6.0 0.0

 TAME (wt%) 0.9 0.8 0.7 1.0 0.1 0.3 0.0

 Ethanol (wt%) 0.0 0.0 0.0 0.0 4.4 4.4 10.2

Aromatics (vol%) 20.4 20.9 21.8 21.4 21.7 22.0 22.1

Benzene (vol%) 0.53 0.56 0.59 0.66 0.62 0.67 0.65

Olefins (vol%) 10.9 11.6 12.1 12.3 13.0 12.1 10.3

Sulfur (ppm) 118 108 101 90 82 65 43

E200 (%off) 47.6 47.0 47.5 47.2 47.6 47.8 45.8

E300 (%off) 84.8 84.4 84.2 83.8 83.5 85.0 85.5

PADD 2 Refineries2

RVP (psi) 6.7 6.8 6.8 6.8 6.9 6.9 7.0

Oxygen (wt%) 3.2 3.2 3.3 3.5 3.5 3.6 3.6

 MTBE (wt%) 2.2 2.1 0.6 0.1 0.0 0.0 0.0

 TAME (wt%) 0.1 0.1 0.0 0.0 0.0 0.0 0.0

 Ethanol (wt%) 8.0 8.0 9.2 10.1 10.2 10.4 10.3

Aromatics (vol%) 17.8 19.4 18.6 17.9 18.5 17.5 17.3

Benzene (vol%) 0.76 0.77 0.71 0.70 0.80 0.82 0.80

Olefins (vol%) 5.4 6.5 6.3 6.6 6.2 5.3 4.9

Sulfur (ppm) 107 126 116 116 84 75 45

E200 (%off) 46.5 46.1 46.1 46.1 47.1 46.9 48.3

E300 (%off) 85.4 84.4 84.4 84.6 83.9 84.0 84.2

PADD 3 Refineries3

RVP (psi) 6.8 6.7 6.8 6.8 6.9 6.9 6.9

Oxygen (wt%) 2.1 2.0 2.1 2.1 2.1 2.0 3.5

 MTBE (wt%) 10.5 10.1 10.5 10.9 11.0 10.3 0.1

 TAME (wt%) 1.1 1.1 0.9 0.9 0.8 0.8 0.0

 Ethanol (wt%) 0.0 0.0 0.0 0.0 0.0 0.0 10.1

Aromatics (vol%) 19.5 19.8 19.9 19.2 21.0 21.0 18.6

Benzene (vol%) 0.60 0.62 0.59 0.61 0.57 0.68 0.53

Olefins (vol%) 10.0 10.4 11.3 11.3 11.2 12.4 10.6

Sulfur (ppm) 156 145 147 132 71 78 41

E200 (%off) 49.1 48.3 48.9 49.9 49.0 50.5 47.8

E300 (%off) 84.0 84.2 83.6 83.6 81.9 83.2 83.9

Note: The estimates are developed by assigning cities included in EPA's area surveys to PADDs

 in which the gasoline likely was produced and then calculating a weighted average

 of gasoline properties (using relative city population). The area surveys do not

 distinguish between imported and domestically-produced gasoline.

2 Estimated from Missouri, Kentucky, Illinois, Indiana, & Wisconsin.

3 Estimated from Texas, Virginia, District of Columbia, & Maryland.

Source: Derived from EPA RFG-Area Surveys, 2000-2006

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-10b: Estimated Properties of Winter RFG, by PADD of Origin

Property 2000 2001 2002 2003 2004 2005 2006

PADD 1 Refineries1

RVP (psi) - - - - - - - 

Oxygen (wt%) 2.0 1.9 1.9 2.0 2.7 2.8 3.5

 MTBE (wt%) 10.0 9.8 9.7 8.9 5.5 4.9 1.1

 TAME (wt%) 0.5 0.4 0.4 0.2 0.1 0.0 0.0

 Ethanol (wt%) 0.3 0.1 0.1 1.1 4.9 5.5 9.5

Aromatics (vol%) 19.3 19.0 20.2 20.2 20.4 20.4 19.6

Benzene (vol%) 0.62 0.61 0.62 0.67 0.71 0.72 0.73

Olefins (vol%) 12.2 13.1 11.9 12.7 12.2 9.9 10.7

Sulfur (ppm) 149 145 142 139 114 84 46

E200 (%off) 56.3 57.2 56.7 56.4 56.5 56.6 58.3

E300 (%off) 86.8 87.5 86.8 86.4 85.3 86.1 87.0

PADD 2 Refineries2

RVP (psi) - - - - - - - 

Oxygen (wt%) 3.4 3.3 3.4 3.6 3.7 3.7 3.7

 MTBE (wt%) 1.5 1.4 0.8 0.1 0.0 0.0 0.0

 TAME (wt%) 0.1 0.1 0.1 0.0 0.0 0.0 0.0

 Ethanol (wt%) 9.0 8.8 9.4 10.4 10.5 10.6 10.7

Aromatics (vol%) 16.0 16.8 17.0 17.2 16.8 16.7 16.4

Benzene (vol%) 0.76 0.79 0.73 0.78 0.77 0.80 0.75

Olefins (vol%) 6.1 6.8 7.0 6.4 6.1 5.4 5.8

Sulfur (ppm) 237 224 225 197 99 91 45

E200 (%off) 59.1 58.5 59.3 58.7 59.4 57.6 59.3

E300 (%off) 85.4 85.0 85.1 85.5 85.0 84.9 85.4

PADD 3 Refineries3

RVP (psi) - - - - - - - 

Oxygen (wt%) 2.0 2.0 2.0 2.0 2.0 2.0 2.9

 MTBE (wt%) 9.9 9.9 10.0 10.2 10.1 10.0 4.4

 TAME (wt%) 1.1 1.2 0.9 0.8 0.8 0.8 0.3

 Ethanol (wt%) 0.0 0.0 0.0 0.0 0.0 0.0 5.9

Aromatics (vol%) 18.0 19.0 19.6 19.0 19.4 18.4 20.0

Benzene (vol%) 0.62 0.62 0.63 0.65 0.57 0.62 0.60

Olefins (vol%) 9.9 10.5 11.1 11.1 11.5 11.2 10.3

Sulfur (ppm) 231 221 223 208 105 84 46

E200 (%off) 54.8 54.4 55.2 55.7 55.6 56.8 55.5

E300 (%off) 84.9 84.3 83.9 83.7 83.4 84.9 84.1

Note: The estimates are developed by assigning cities included in EPA's area surveys to PADDs

 in which the gasoline likely was produced and then calculating a weighted average

 of gasoline properties (using relative city population). The area surveys do not

 distinguish between imported and domestically-produced gasoline.

1 Estimated from Pennsylvania, New York, New Jersey, & Delaware.

2 Estimated from Missouri, Kentucky, Illinois, Indiana, & Wisconsin.

3 Estimated from Texas, Virginia, District of Columbia, & Maryland.

Source: Derived from EPA RFG-Area Surveys, 2000-2006

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-11: Gasoline Produced by California Refineries -- 

Volume and Average Properties, by Type and GradeSummer 20061

California RFG 

CARBOB Finished2 Arizona CBG All Other 

Prem Reg Pool Prem Reg Pool Prem Reg 17.1% Pool Prem Reg 12.0

Volume (K b/d) 161 724 884 170 767 937 1 53 54 21 116 

PropertiesRVP (psi) 5.6 5.6 5.6 6.8 6.8 6.8 6.8 6.7 6.7 6.7 8.0 8.0 Oxygen (wt%) 2.0 2.0 2.0Aromatics (vol%) 23.7 24.8 24.6 22.5 23.5 23.3 22.3 25.8 25.2 25.7 30.3 30.9 3Benzene (vol%) 0.51 0.59 0.58 0.48 0.56 0.55 0.36 0.71 0.65 0.71 0.44 0.63 0Olefins (vol%) 6.1 5.9 5.9 5.8 5.6 5.6 2.2 11.1 9.6 11.0 6.7 6.8 Sulfur (ppm) 7 10 10 7 10 9 6 22 19.4 22 5 26 2T50 217 214 215 214 210 211 220 217 218 217 227 222 T90 309 312 311 307 309 309 321 321 321 321 315 332 E200 (est) 39.2 42.5 41.9 43.3 46.4 45.8 35.0 42.5 41.2 42.4 37.6 43.2 4E300 (est) 88.0 87.0 87.2 88.9 88.0 88.1 85.5 85.5 85.5 85.5 85.6 79.0 7API Gravity 60.5 59.3 59.5 59.7 58.6 58.8 63.2 59.0 59.7 59.0 58.0 57.4 5Distillation (°F)IBP 103 106 106 91 100 100 95 93 T10 151 149 149 152 142 142 136 132 T30 184 180 181 193 174 174 185 156 T50 217 214 215 214 210 211 220 217 217 227 223 T70 249 252 251 254 255 255 264 277 T90 309 312 311 307 309 309 321 321 321 314 331 FBP 384 381 382 390 400 400 387 401 OctaneMON 85.6 81.8 82.5 86.6 83.1 83.7 88.2 83.0 83.9 83.0 86.5 82.9 8RON 93.3 88.6 89.5 95.0 90.6 91.4 94.7 91.4 92.0 91.4 95.8 91.6 9CON 89.4 85.2 86.0 90.8 86.8 87.6 91.5 87.2 87.9 87.2 91.1 87.2 8Octane w 10% EthanolMON 84.7 80.7 81.4RON 91.8 86.9 87.8CON 88.2 83.8 84.6

1 The CEC Survey covered June 1 through September 30, 2006 (122 calendar days).Source: Derived from CEC 2007 Survey of California Refineries.

October 8, 2010 
Single Octane NCG

Exhibit A-12a: Estimated Average Gasoline Properties, by Gasoline Type and Producing-Region --

Summer 2004-2008

PADD 1 PADD 2 PADD 3 

2004 2006 2007 2008 2004 2006 2007 2008 2004 2006 2007 2008 2004 

RFGRVP (psi) 7.0 6.9 6.8 6.8 7.0 7.0 7.1 7.6 6.9 6.9 6.9 6.9 7Oxygen (wt %) 2.7 3.3 3.3 3.4 3.4 3.3 3.4 3.2 2.1 3.3 3.4 3.4 1

 MTBE (vol %) 7.66 0.00 0.17 0.00 0.00 0.00 0.00 0.00 10.77 0.00 0.00 0.00 0 TAME (vol %) 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.8 0.0 0.0 0.0  Ethanol (vol %) 3.75 9.37 9.34 9.78 9.59 9.42 9.61 9.08 0.00 9.30 9.59 9.79 4

Aromatics (vol %) 24.2 23.4 24.0 21.4 20.7 17.3 16.8 20.3 23.5 20.2 18.8 18.7 22Benzene (vol %) 0.52 0.63 0.69 0.60 0.77 0.82 0.68 0.83 0.55 0.60 0.56 0.58 0.Olefins (vol %) 13.6 10.0 9.9 10.0 7.2 3.7 4.8 6.8 11.3 10.8 10.5 11.1 5Sulfur (pm) 95 33 28 29 97 38 27 26 80 39 21 25 E200 (% off) 48.7 44.7 44.5 46.4 46.4 47.3 47.9 51.3 49.5 48.0 48.0 48.3 44E300 (% off) 82.5 84.2 83.6 86.9 83.0 83.5 83.2 85.0 81.6 83.0 83.6 85.3 87CGRVP (psi) 7.7 7.6 7.4 7.3 8.3 8.4 8.5 8.4 7.4 7.6 7.6 7.5Oxygen (wt %) 1.0 0.5 0.5 0.5 1.0 1.7 2.5 3.3 0.1 0.0 0.0 0.7

 MTBE (vol %) 2.99 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.49 0.00 0.00 0.00 TAME (vol %) 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.2 0.0 0.0 0.0 Ethanol (vol %) 1.34 1.33 1.55 1.31 3.00 4.72 7.07 9.30 0.03 0.03 0.14 2.05

Aromatics (vol %) 30.5 33.4 30.4 30.8 29.6 29.1 28.7 26.0 31.8 31.9 29.3 27.7Benzene (vol %) 0.71 0.90 1.04 0.81 1.19 1.37 1.24 1.15 0.97 1.13 1.09 0.95Olefins (vol %) 10.8 10.6 10.4 11.1 8.7 7.4 7.1 8.0 10.4 10.0 9.9 14.4Sulfur (pm) 113 40 35 29 154 62 36 39 92 38 37 30E200 (% off) 43.3 42.8 41.6 44.7 44.6 46.4 48.4 51.9 43.2 41.6 42.2 42.8E300 (% off) 80.7 81.0 82.2 84.2 80.6 81.9 81.8 84.1 79.6 78.9 79.6 81.3

Note: Pool properties estimated using regional premium/regular grade splits for 2007.Source: Derived from Alliance North American Gasoline Surveys, Summer and Winter, 2004 - 2009.

October 8, 2010 
Single Octane NCG

Exhibit A-12b: Estimated Average Gasoline Properties, by Gasoline Type and Producing-Region --

Winter 2004-2008

PADD 1 PADD 2 PADD 3 

2004 2006 2007 2008 2004 2006 2007 2008 2004 2006 2007 2008 2004 

RFGRVP (psi) 13.4 13.3 13.1 12.7 13.7 13.3 13.5 13.2 12.2 12.6 12.3 12.4 11Oxygen (wt %) 2.4 3.5 3.5 3.4 3.3 3.5 3.4 3.2 1.9 3.5 3.5 3.4 1

 MTBE (vol %) 5.81 0.00 0.00 0.00 0.05 0.00 0.00 0.00 9.58 0.00 0.00 0.00 0 TAME (vol %) 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 1.0 0.0 0.0 0.0  Ethanol (vol %) 3.71 9.99 9.93 9.81 9.51 9.99 9.81 9.01 0.00 10.09 10.09 9.62 5

Aromatics (vol %) 21.7 22.0 18.6 19.6 17.4 16.6 15.1 19.2 19.7 19.3 17.5 18.2 20Benzene (vol %) 0.60 0.67 0.83 0.71 0.67 0.73 0.76 0.85 0.60 0.66 0.72 0.58 0.Olefins (vol %) 11.7 10.9 13.0 10.1 6.1 6.2 6.6 5.1 10.1 9.3 10.4 9.0 4Sulfur (pm) 100 34 36 31 96 46 33 46 123 31 26 31 E200 (% off) 54.9 55.0 56.2 57.6 58.8 57.9 57.4 59.1 58.0 56.4 56.8 56.8 50E300 (% off) 84.2 83.6 85.2 88.5 84.9 85.2 84.2 85.5 83.0 82.3 84.4 86.1 87CGRVP (psi) 14.0 13.5 13.3 12.4 13.2 14.5 14.6 14.6 12.6 12.4 12.2 12.2Oxygen (wt %) 0.0 0.0 0.7 3.5 0.9 1.9 3.0 3.4 0.2 0.1 0.2 1.8

 MTBE (vol %) 0.13 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.61 0.00 0.00 0.00 TAME (vol %) 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 Ethanol (vol %) 0.00 0.00 1.96 9.89 2.54 5.33 8.46 9.57 0.20 0.21 0.51 5.24

Aromatics (vol %) 30.1 27.3 21.9 20.2 22.1 22.7 21.0 22.3 25.8 25.0 26.4 23.7Benzene (vol %) 1.16 0.99 0.97 0.86 1.12 1.19 1.32 1.13 1.00 0.97 1.12 0.98Olefins (vol %) 5.6 11.0 11.5 8.8 6.6 7.7 8.6 8.1 10.3 11.5 11.4 10.1Sulfur (pm) 29 24 19 37 140 40 47 57 140 32 31 33E200 (% off) 48.0 48.4 52.2 57.3 48.6 56.3 59.1 60.1 50.0 50.0 50.1 51.9E300 (% off) 81.9 81.6 84.7 87.2 75.4 85.2 85.9 87.8 81.4 82.3 81.5 85.9

Note: Pool properties estimated using regional premium/regular grade splits for 2007.Source: Derived from Alliance North American Gasoline Surveys, Summer and Winter, 2004 - 2009.

October 8, 2010 
Single Octane NCG

Exhibit A-13: Estimated Octane of Gasoline by Producing Region, Season, and Type and Grade of Gasoline

Summer Winter

Producing Gas Premium Regular Premium 

Region Type Year RON MON (R+M)/2 RON MON (R+M)/2 RON MON (R+M)/2 RO

PADD 1 RFG Average 98.3 87.2 92.8 92.6 82.9 87.7 98.4 86.9 92.6 

2006 98.8 87.2 93.0 93.2 83.5 88.3 97.8 86.7 92.2 2007 98.3 87.2 92.7 92.5 82.6 87.6 98.7 87.5 93.1 2008 97.9 87.2 92.6 92.1 82.6 87.3 98.7 86.4 92.6 

CG Average 98.6 87.3 92.9 92.3 82.7 87.5 98.3 87.6 92.9 

2006 98.2 87.0 92.6 92.2 82.7 87.5 97.7 87.3 92.5 2007 98.7 87.7 93.2 92.2 82.8 87.5 98.2 88.4 93.3 2008 98.8 87.3 93.0 92.5 82.6 87.6 99.0 87.2 93.0 

PADD 2 RFG Average 97.6 87.9 92.7 92.0 84.0 88.0 97.8 88.1 93.0 

2006 98.6 88.6 93.6 91.5 85.2 88.3 98.1 88.0 93.0 2007 96.1 87.1 91.6 92.0 83.6 87.8 98.2 88.5 93.4 2008 98.1 87.9 93.0 92.6 83.1 87.9 97.3 87.8 92.5 

CG Average 98.2 87.6 92.9 93.4 83.5 88.5 98.0 87.6 92.8 

2006 98.3 87.5 92.9 92.8 83.4 88.1 97.6 87.6 92.6 2007 97.9 87.6 92.8 93.6 83.6 88.6 98.0 87.7 92.8 2008 98.2 87.7 93.0 93.8 83.5 88.7 98.4 87.4 93.0 

PADD 3 RFG Average 98.6 87.6 93.1 92.1 83.0 87.5 98.4 87.3 92.8 

2006 99.0 87.8 93.4 92.1 83.1 87.6 98.1 87.7 92.9 2007 98.6 87.9 93.2 92.2 83.0 87.6 98.6 87.4 93.0 2008 98.3 87.2 92.8 92.0 82.7 87.4 98.5 86.7 92.6 

CG Average 97.6 88.1 92.9 92.3 82.7 87.5 97.8 87.9 92.8 

2006 97.5 87.8 92.7 92.1 82.5 87.3 98.0 87.8 92.9 2007 97.5 88.3 92.9 91.8 82.4 87.1 97.6 88.4 93.0 2008 97.9 88.2 93.1 93.1 83.2 88.1 97.8 87.5 92.7 

PADD 4&5 CG Average 96.8 86.4 91.6 91.1 82.5 86.8 96.8 87.1 91.9 

2006 96.8 86.5 91.6 90.7 82.5 86.6 96.3 86.9 91.6 2007 97.1 86.7 91.9 91.1 82.2 86.7 96.6 86.9 91.8 2008 96.4 86.1 91.2 91.4 82.9 87.1 97.3 87.4 92.3 

California RFG Average 95.9 86.9 91.4 91.5 83.1 87.3 96.1 86.6 91.3 

2006 95.6 86.8 91.2 91.4 83.0 87.2 96.3 86.6 91.5 2007 95.9 87.0 91.4 91.6 83.1 87.3 96.1 86.6 91.3 2008 96.0 86.9 91.4 91.6 83.1 87.3 96.0 86.4 91.2 

Source: Derived from Alliance North American Gasoline Surveys, Summer and Winter, 2006 - 2009.

October 8, 2010 
Single Octane NCG

Exhibit A-14: Gasoline Grade Splits, by Consuming Region

and Gasoline Type

Conventional &

RFG Oxygenated

Region Year Prem Reg Prem Reg

PADD 1 2000 24% 76% 19% 81%

2001 23% 77% 18% 82%

2002 23% 77% 18% 82%

2003 21% 79% 16% 84%

2004 19% 81% 14% 86%

2005 17% 83% 12% 88%

2006 15% 85% 11% 89%

2007 14% 86% 11% 89%

2008 13% 87% 9% 91%

PADD 2 2000 18% 82% 13% 87%

2001 17% 83% 12% 88%

2002 17% 83% 12% 88%

2003 16% 84% 11% 89%

2004 14% 86% 10% 90%

2005 13% 87% 10% 90%

2006 12% 88% 9% 91%

2007 11% 89% 9% 91%

2008 10% 90% 9% 91%

PADD 3 2000 19% 81% 15% 85%

2001 18% 82% 14% 86%

2002 18% 82% 14% 86%

2003 16% 84% 13% 87%

2004 14% 86% 11% 89%

2005 13% 87% 9% 91%

2006 12% 88% 8% 92%

2007 11% 89% 8% 92%

2008 10% 90% 7% 93%

PADDs 4&5 2000 16% 84% 16% 84%

ex CA 2001 16% 84% 16% 84%

2002 16% 84% 17% 83%

2003 14% 86% 16% 84%

2004 13% 87% 14% 86%

2005 14% 86% 13% 87%

2006 13% 87% 12% 88%

2007 14% 86% 13% 87%

2008 12% 88% 12% 88%

California 2000 19% 81%

2001 19% 81%

2002 20% 80%

2003 19% 81%

2004 18% 82%

2005 17% 83%

2006 17% 83%

2007 17% 83%

2008 16% 84%

U.S. 2000 21% 79% 16% 84%

2001 20% 80% 15% 85%

2002 20% 80% 15% 85%

2003 19% 81% 14% 86%

2004 17% 83% 12% 88%

2005 16% 84% 11% 89%

2006 15% 85% 10% 90%

2007 15% 85% 10% 90%

2008 13% 87% 9% 91%

Note: 60% and 40% of mid-grade allocated to regular and premium, respectively.

Source: Derivived from Prime Supplier Sales, EIA Website.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-15: Distribution of Summer Gasoline, by Type of Gasoline and Region --

Current and Projected under the 8-Hour Ozone Standard

Gasoline Type

EtOH

Conven- Mandate Low RVP Federal Calif. Arizona

Region tional (Minn.) 7.8 7.01 RFG RFG CBG Total

Current 44.9% 2.6% 14.9% 2.5% 23.2% 11.0% 0.8% 100.0%

PADD 1 42.3% 14.2% 5.2% 38.3% 100.0%

Subdistrict 1A 12.3% 6.4% 81.3% 100.0%

Subdistrict 1B 30.3% 6.0% 63.8% 100.0%

Subdistrict 1C 58.7% 22.2% 10.3% 8.8% 100.0%

PADD 2 64.3% 6.9% 10.2% 2.9% 15.8% 100.0%

PADD 3 45.6% 27.5% 4.5% 22.5% 100.0%

PADDs 4 & 5 ex CA 59.0% 33.3% 0.7% 7.1% 100.0%

California 100.0% 100.0%

Projected 33.4% 2.6% 22.1% 5.5% 24.4% 11.0% 0.9% 100.0%

PADD 1 27.2% 24.3% 4.9% 43.5% 100.0%

Subdistrict 1A 11.6% 7.2% 81.3% 100.0%

Subdistrict 1B 7.7% 28.2% 64.1% 100.0%

Subdistrict 1C 45.4% 26.0% 9.6% 19.0% 100.0%

PADD 2 43.9% 6.9% 19.2% 11.2% 18.9% 100.0%

PADD 3 45.4% 26.0% 4.6% 24.0% 100.0%

PADDs 4 & 5 ex CA 43.9% 7.1% 40.1% 8.2% 100.0%

California 100.0% 100.0%

Note: Gasoline is classified by the area into which it is sold. Gasoline shares for the summer are estimated using annual data, 

 on the assumption that relative sales of gasoline in geographic areas are the same across seasons.

1 Assumes small area with 7.2 RVP gasoline shifts to 7.0 RVP.

Source: Derived from Exhibit B-8, "Refining Economics of a National Clean Gasoline Standard for PADDs 1-3,"

 for the Alliance of Automobile Manufacturers, MathPro Inc., 05/07/07; and Prime Supplier Gasoline Sales, 2007,

 EIA Website.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-16: Estimated Distribution of Summer

Conventional and Low-RVP Gasoline

and Pool RVP, 2007

Gasline Distribution (%) Average

Conven- Low RVP RVP

Region tional 7.8 7.01 Total (psi)

Within Region Use 73% 23% 4% 100%

PADD 1 69% 23% 8% 100%

Subdistrict 1A 66% 34% 100%

Subdistrict 1B 84% 16% 100%

Subdistrict 1C 64% 24% 11% 100%

PADD 2 84% 12% 3% 100%

PADD 3 59% 35% 6% 100%

PADDs 4 & 5 ex CA 64% 36% 100%

California 0%

Refinery Production 73% 23% 4% 100%

PADD 1 48% 52% 100% 8.1

PADD 2 86% 11% 3% 100% 8.7

PADD 3 70% 25% 6% 100% 8.3

PADDs 4 & 5 ex CA 52% 48% 100% 8.3

California 35% 65% 100% 8.0

Note: Average RVP reflects the effects of the 1 psi ethanol RVP waiver, except for 

 low-RVP gasoline during July and August. 

Source: Derived from Exhibit A-14 and Exhibit B-6c, "Refining Economics of a National Clean

 Gasoline Standard for PADDs 1-3," for The Alliance of Automobile Manufacturers,

 MathPro Inc., 05/07/07.

October 8, 2010 MathPro
Single Grade NCG

Exhibit A-17a: Distribution of Refining Regions' Gasoline Production, Estimated

Grade Splits, and Pool Octane, by PADD -- 2007

Supplying Share of Production Shipped To: Premium Pool Octane

Region PADD 1 PADD 2 PADD 3 PADD 4 PADD 5 Grade Split RON MON (R

PADD 1Reformulated 100% 14.5% 93.5 83.4 All Other 100% 10.9% 92.9 83.3 PADD 2Reformulated 97% 3% 11.5% 92.6 84.2 All Other 1% 95% 2% 2% 11.6% 93.8 83.9 PADD 3Reformulated 35% 16% 38% 11% 13.1% 92.9 83.4 All Other 48% 14% 35% 2% 2% 8.5% 92.7 83.2 PADD 4-5 ex CA

ReformulatedAll Other 6% 86% 8% 13.4% 91.8 83.1 CaliforniaCARBOB 100% 17.1% 89.4 82.4 Reformulated 100% 17.1% 92.4 83.7 All Other 100% 12.0% 93.5 83.4 

Note: The premium grade split includes 40% of the mid-grade share. Premium shares for conventional gasoline are adjusted to reflect no shipments of premium from PADD 3 to PADD 2Source: Derived from Exhibits A-10, A-12, A-13 & A-14; and Tables 2, 4, 6, 8, 12 and 34, Petroleum Supply Annual, 2007, EIA/DOE.

October 8, 2010 
Single Grade NCG

Exhibit A-17b: Distribution of Refining Regions' Gasoline Production, Estimated

Grade Splits, and Pool Octane, by PADD -- 2008

Supplying Share of Production Shipped To: Premium Pool Octane

Region PADD 1 PADD 2 PADD 3 PADD 4 PADD 5 Grade Split RON MON (R

PADD 1Reformulated 100% 12.9% 93.4 83.3 All Other 100% 9.0% 92.8 83.2 PADD 2Reformulated 97% 3% 10.4% 92.6 84.1 All Other 1% 96% 2% 2% 11.1% 93.8 83.9 PADD 3Reformulated 34% 13% 40% 13% 11.6% 92.8 83.4 All Other 49% 14% 35% 1% 1% 7.9% 92.7 83.1 PADD 4-5 ex CA

ReformulatedAll Other 7% 84% 9% 12.5% 91.7 83.1 CaliforniaCARBOB 100% 15.7% 89.4 82.4 Reformulated 100% 15.7% 92.4 83.7 All Other 100% 11.1% 93.5 83.4 

Note: The premium grade split includes 40% of the mid-grade share. Premium shares for conventional gasoline are adjusted to reflect no shipments of premium from PADD 3 to PADD 2Source: Derived from Exhibits A-10, A-12, A-13 & A-14; and Tables 2, 4, 6, 8, 12 and 34, Petroleum Supply Annual, 2007, EIA/DOE.

October 8, 2010 
Single Octane NCG

Exhibit A-18: Refiner's Average Crude Oil Acquisition Cost,

by PADD

($/b)

PADD 1 PADD 2 PADD 3 PADD 4 PADD 5 U.S.

2005 53.26 50.63 49.30 50.59 50.60 50.32

Summer 54.85 52.54 51.85 52.45 52.69 52.53

Winter 58.88 54.40 54.03 53.72 55.47 55.06

2006 63.58 59.51 59.42 58.05 60.91 60.10

Summer 67.81 64.83 64.01 63.65 63.34 64.83

Winter 58.05 54.12 53.62 51.74 53.47 54.28

2007 72.18 67.16 67.57 63.49 68.14 67.98

Summer 71.63 65.92 66.54 62.90 67.37 66.96

Winter 90.45 86.69 87.38 81.78 87.69 87.58

2008 96.47 95.20 93.44 89.84 94.78 94.30

Summer 118.62 116.59 114.22 111.33 108.80 115.47

Winter 49.43 47.96 47.51 43.27 41.11 47.73

Projected 20151 105.30 100.51 99.49 96.63 101.22 100.58

Notes: Summer season defined as April through September for PADDs 1-4 and U.S. and

 March through October for PADD 5. Winter season defined as October through

 March for PADDs 1-4 and U.S. and November through February for PADD 5.

 Winter season extends across years.

1 The projected U.S. crude oil acquisition cost is estimated as 1.04 times EIA's projected price

 of imported crude oils. Regional crude oil acquisition costs are estimated using the

 average ratios of regional to U.S. crude oil acquisition costs from 2005 to 2008.

Source: Derived from Crude Oil Acquisition Cost, EIA Website; and Annual Energy Outlooks,

 2006-2009, EIA/DOE.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-19: Refined Product (and WTI) Spot Prices, by Region

($/b)

PADD 1 PADD 3 

Regular Distillate Residual Regular Distillate Residual 

Gasoline Kero EPA Heating Oil Gasoline Kero EPA Heating Oil WTI R

CG RBOB Jet Diesel Oil (1% Sulf) CG RBOB Jet Diesel Oil (1% Sulf) Propane Cushing CA

2005 65.46 71.86 70.26 68.10 41.51 66.76 71.83 70.59 68.04 38.20 38.33 56.49 Summer 70.15 73.64 72.21 69.68 42.79 72.20 73.29 72.50 69.56 40.73 37.70 58.12 Winter 68.45 78.08 76.39 73.18 48.03 69.10 78.87 77.69 74.01 44.22 42.18 61.63 2006 76.52 79.13 81.95 81.55 75.74 46.14 76.61 80.67 81.41 75.84 44.67 42.56 66.02 Summer 84.70 89.24 87.70 88.00 80.45 48.13 85.09 89.60 86.26 88.10 80.77 46.74 45.28 70.41 Winter 68.41 68.24 75.06 74.00 69.59 40.24 66.79 67.05 73.66 73.67 68.83 40.44 40.34 59.03 2007 86.49 87.60 90.92 89.18 85.33 54.07 85.59 87.42 89.46 88.89 84.30 55.67 50.72 72.32 Summer 89.45 91.99 90.01 88.04 83.82 53.75 89.78 93.05 88.71 87.96 83.11 55.69 49.47 70.22 Winter 98.99 98.37 115.28 112.80 109.97 70.72 98.28 99.20 112.73 111.63 108.09 71.44 62.46 94.35 2008 102.83 104.05 127.38 122.60 119.81 76.09 103.69 107.15 124.39 121.10 117.96 77.95 59.31 99.57 Summer 126.01 129.45 152.83 146.91 143.36 93.67 128.94 134.78 150.59 145.89 142.25 96.50 71.02 121.00 Winter 54.66 53.33 70.24 67.33 66.54 41.00 52.86 53.14 66.96 64.73 63.96 43.79 31.03 50.63 

Sources: Derived from Average Monthly Spot Prices, EIA Website; and Average Monthly Prices for CARB diesel, OPIS.

October 8, 2010 
Single Octane NCG

Exhibit A-20a: Seasonal Average Wholesale/Resale Prices for Reformulated Gasoline by All Sellers

($/b)

PADD 1 PADD 2 PADD 3 PADD 4 PADD 5 California 

Reg Prem Reg Prem Reg Prem Reg Prem Reg Prem Reg Prem R

2000 40.97 46.15 42.60 48.20 38.85 42.16 44.15 49.63 44.23 49.71 Summer 42.85 48.23 45.22 50.95 40.87 44.21 46.25 51.65 46.42 51.82 Winter 40.29 45.53 40.83 46.10 37.63 41.17 43.60 49.15 43.52 49.07 2001 37.22 43.24 40.53 46.28 35.38 39.44 41.66 47.57 41.75 47.68 Summer 41.37 47.81 46.22 52.38 39.42 43.62 45.16 51.29 45.36 51.52 Winter 27.17 32.91 29.69 34.98 25.91 29.97 27.69 32.98 27.59 32.90 2002 34.41 40.58 37.16 42.45 33.33 36.80 37.74 43.24 37.78 43.29 Summer 36.35 42.57 39.78 45.35 35.36 38.89 39.88 45.40 39.94 45.47 Winter 40.78 46.96 42.68 47.66 39.40 42.76 42.35 47.89 42.42 47.97 2003 42.23 48.36 44.37 49.37 39.93 44.04 48.87 54.40 48.78 54.35 Summer 41.89 48.23 44.41 49.49 39.37 43.68 50.71 56.31 50.58 56.24 Winter 44.09 49.98 45.46 50.25 41.73 45.75 47.60 52.96 47.45 52.85 2004 53.98 60.06 55.47 60.35 51.99 56.42 61.68 67.34 61.67 67.33 Summer 56.29 62.74 58.04 63.07 54.32 58.74 64.49 70.07 64.50 70.05 Winter 56.57 62.09 58.20 62.81 55.15 59.83 60.20 66.13 60.15 66.11 2005 69.63 76.78 71.17 75.79 69.65 74.12 74.98 80.73 74.81 80.59 Summer 75.19 82.46 75.95 80.58 74.46 78.91 80.00 85.90 79.84 85.77 Winter 72.28 80.32 74.24 78.93 73.89 78.18 72.91 78.47 72.66 78.26 2006 83.85 91.62 83.92 89.34 83.25 88.76 87.88 94.06 87.94 94.10 Summer 95.69 103.99 95.55 101.19 94.33 99.97 93.90 100.23 94.06 100.35 Winter 72.80 80.21 71.69 77.49 71.77 78.57 78.12 84.67 78.20 84.75 2007 90.67 99.28 93.27 99.80 90.31 98.90 96.87 104.22 97.09 104.42 Summer 95.26 104.61 101.12 108.02 95.39 104.46 98.97 106.42 99.18 106.63 Winter 100.64 108.40 100.43 106.76 101.10 110.10 103.95 111.07 104.10 111.20 12008 107.42 116.33 110.38 117.05 107.91 116.86 112.25 119.29 112.30 119.37 1Summer 130.68 140.01 135.83 142.53 131.90 140.88 128.92 135.95 129.04 136.10 1Winter 59.80 68.35 61.49 68.27 59.30 68.14 58.56 65.47 58.47 65.42 

Notes: Winter season runs across years; PADD 5 and California winter season runs from November through February.Source: Derived from Gasoline Prices by Formulation, Grade, and Sales Type, EIA Website

October 8, 2010 
Single Octane NCG

Exhibit A-20b: Seasonal Average Wholesale/Resale Prices for Conventional Gasoline by All Sellers

($/b)

PADD 1 PADD 2 PADD 3 PADD 4 PADD 5 California 

Reg Prem Reg Prem Reg Prem Reg Prem Reg Prem Reg Prem R

2000 37.89 42.22 38.83 42.96 36.66 40.42 41.06 45.14 43.00 48.88 Summer 38.93 43.56 40.21 44.49 37.79 42.04 42.51 46.58 45.01 50.73 Winter 37.42 41.84 37.99 42.06 36.21 39.91 40.52 44.59 41.58 47.86 2001 33.89 38.62 36.36 40.52 33.19 37.23 38.58 42.86 39.46 45.56 Summer 36.91 41.89 41.15 45.40 36.18 40.59 42.77 47.01 41.77 47.70 Winter 25.82 30.06 26.63 30.77 25.24 28.77 29.28 33.64 28.67 35.19 2002 32.62 37.24 33.63 38.02 31.85 35.96 35.21 39.64 35.63 41.28 Summer 34.21 39.05 35.55 40.08 33.54 37.92 37.52 42.00 37.35 42.87 Winter 38.91 43.43 39.41 43.73 38.08 41.84 40.40 44.86 39.45 45.05 2003 39.57 44.03 40.60 45.09 38.80 43.03 42.58 47.03 43.91 49.91 Summer 38.73 43.27 40.59 45.17 38.19 42.50 42.98 47.40 44.84 50.98 Winter 42.15 46.43 41.94 46.41 40.64 45.22 43.43 48.00 43.90 49.44 2004 52.05 56.71 52.11 56.87 50.60 55.47 54.16 58.64 56.21 61.75 Summer 53.77 58.56 54.25 59.22 52.50 57.67 57.21 61.57 58.76 64.21 Winter 55.89 60.75 56.17 60.82 54.37 58.86 56.74 61.41 55.92 61.90 2005 68.33 74.10 68.83 73.84 67.42 72.33 70.37 75.13 72.87 78.76 Summer 72.46 78.55 73.22 78.42 71.24 76.56 76.41 81.12 78.05 83.85 Winter 72.19 78.01 72.13 77.13 72.09 77.44 71.49 76.26 69.95 76.02 2006 79.84 86.94 80.48 86.42 79.29 86.42 82.62 87.78 85.91 92.18 Summer 88.82 96.63 90.08 96.31 88.57 96.04 93.50 98.80 91.48 97.95 Winter 70.06 77.06 69.90 76.01 68.56 76.15 71.93 77.26 76.99 83.56 2007 88.77 97.13 91.28 98.30 87.22 96.46 92.67 99.35 94.15 101.39 Summer 92.86 102.38 97.92 105.41 91.91 102.25 100.07 107.12 96.72 103.93 Winter 101.26 109.07 100.76 107.89 99.25 107.52 101.00 108.31 102.04 109.37 12008 107.42 116.19 107.03 114.39 106.17 114.64 108.89 116.11 110.82 117.67 1Summer 130.67 139.51 131.17 138.70 129.11 138.09 134.80 142.07 127.29 134.09 1Winter 59.07 68.04 58.50 65.74 57.83 66.30 56.57 63.47 56.58 63.50 

Notes: Winter season runs across years; PADD 5 and California winter season runs from November through February.Source: Derived from Gasoline Prices by Formulation, Grade, and Sales Type, EIA Website

October 8, 2010 
Single Octane NCG

Exhibit A-20c: Seasonal Average Wholesale/Resale Prices for No. 2 Diesel by All Sellers, by Sulfur Level

($/b)

PADD 1 PADD 2 PADD 3 PADD 4 PADD 5 

15 to 15 to 15 to 15 to 15 to 

< 15 ppm 500 ppm > 500 < 15 ppm 500 ppm > 500 < 15 ppm 500 ppm > 500 < 15 ppm 500 ppm > 500 < 15 ppm 500 ppm > 50

2000 37.8 36.7 37.9 37.7 36.0 34.8 40.5 40.3 41.2 4Summer 36.4 35.1 37.6 37.4 35.4 33.9 39.7 39.4 41.0 3Winter 39.0 38.3 38.8 38.8 37.4 36.3 42.6 43.0 42.8 42001 32.1 31.5 34.7 34.4 31.4 30.3 36.7 35.7 34.6 3Summer 33.4 32.6 37.2 36.4 33.2 31.9 39.3 38.2 36.0 3Winter 25.6 24.9 26.8 27.2 24.5 24.0 27.5 26.6 25.0 22002 30.4 29.3 31.2 30.8 29.6 28.6 32.4 31.8 31.8 3Summer 30.8 29.7 31.7 31.2 30.1 29.2 33.3 32.6 32.8 3Winter 39.2 37.5 39.1 38.0 37.9 36.2 40.3 40.1 38.3 32003 37.7 36.3 37.8 37.2 36.5 35.0 40.5 40.6 39.4 3Summer 35.0 33.9 35.8 35.4 34.1 32.6 38.9 39.1 38.6 3Winter 39.4 37.5 39.2 38.9 38.5 36.8 42.1 42.4 42.5 42004 49.5 47.3 49.4 48.7 48.5 46.5 53.6 53.3 55.5 5Summer 48.0 45.8 48.6 47.9 47.4 45.2 54.6 55.2 57.8 5Winter 60.5 58.5 59.7 59.0 58.5 57.2 62.7 63.6 58.9 52005 72.3 69.3 73.4 72.1 72.1 69.1 77.7 79.5 76.5 7Summer 73.7 70.4 74.0 72.9 73.1 69.9 79.2 82.1 80.8 8Winter 79.6 75.7 81.6 79.2 80.7 76.1 85.0 85.3 77.9 72006 84.1 77.9 85.8 82.9 84.2 78.0 91.4 92.2 88.8 8Summer 90.4 82.7 92.8 89.4 90.9 83.6 99.4 100.4 91.7 9Winter 76.9 72.4 79.2 76.4 76.2 70.3 85.0 84.0 82.1 82007 92.9 91.3 88.1 94.3 93.1 92.3 91.6 90.2 86.6 100.3 99.4 95.2 93.5 9Summer 92.2 90.3 87.0 94.4 92.7 91.4 91.4 89.4 86.3 100.5 98.6 94.5 93.0 9Winter 116.4 114.3 112.7 114.9 114.0 116.8 112.3 113.0 110.1 118.4 119.6 110.9 109.7 112008 127.8 125.5 126.8 126.2 125.4 129.4 125.0 125.2 122.1 130.2 131.5 123.9 123.9 Summer 151.4 149.5 150.7 149.7 148.6 153.8 148.7 149.1 145.3 155.4 156.5 141.2 141.8 Winter 74.1 71.2 73.6 71.8 71.9 74.6 70.9 70.3 70.0 75.3 75.6 63.9 63.0 

Notes: Winter season runs across years; pink indicates California seasons.Source: Derived from No. 2 Distillate Prices by Sales Type, EIA Website

October 8, 2010 
Single Octane NCG

Exhibit A-21: Spot Prices for C4s and C5s

($/b)

Mont Belview, TX Los Angeles

Iso- IsoButane Butane C5s Butane Butane

2003 28.13 29.02 30.72

Summer 25.08 26.36 27.87

Winter 31.25 30.75 33.90

2004 36.78 36.86 41.92

Summer 36.01 35.96 41.47

Winter 42.16 42.89 48.25

2005 45.85 48.39 52.92 46.73 58.93

Summer 44.46 47.63 53.12 37.99 54.80

Winter 51.79 54.77 57.81 55.48 63.06

2006 50.52 51.99 60.52 44.70 58.60

Summer 52.49 53.69 64.24 42.72 59.47

Winter 47.18 49.19 56.40 46.69 57.74

2007 59.73 62.55 70.55 57.93 77.24

Summer 58.04 61.65 70.04 45.95 66.97

Winter 75.53 77.16 86.93 69.92 87.51

2008 70.62 72.39 87.92 45.45 67.53

Summer 84.36 85.41 108.40 66.19 88.85

Winter 38.08 41.01 43.81 24.72 46.22

Projected 20151 77.26 79.35 94.33 67.02 88.66

Summer 75.09 77.14 94.33 60.50 83.88

Winter 79.44 81.55 94.33 73.54 93.45

Note: Winter season extends across years.

1 Projected prices based on a projected WTI price of about $104/b and historical

 relationships between WTI, C4 and C5 prices.

Source: Average Monthly Prices for C4s and C5s, OPIS.

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-22: Annual Average Price of Natural Gas to Industrial Users, by Region

($/mcf)

Projected

Region 2000 2001 2002 2003 2004 2005 2006 2007 2008 20151

PADD 1 5.10 6.90 5.70 7.52 8.66 10.72 11.43 10.01 6.96 5.29

PADD 2 5.24 6.94 5.30 7.25 8.08 10.08 9.79 9.20 8.44 6.42

PADD 3 4.05 4.65 3.52 5.39 6.11 8.10 7.00 6.87 8.87 6.75

PADD 4 5.15 5.75 4.05 4.81 6.36 8.07 9.98 7.59 8.62 6.56

PADD 5 4.80 5.89 4.75 6.49 7.41 9.35 9.18 9.13 10.80 8.21

California 5.29 6.60 4.93 7.19 7.89 9.84 9.30 9.07 10.71 8.14

U.S. 4.57 5.60 4.33 6.15 6.99 8.98 8.49 8.08 8.95 6.80

Note: Regional averages are calculated by weighting state prices by the distribution of crude oil distillation capacity.

1 Projected regional prices are based on the projected U.S. price and regional to national price ratios in 2008.

Source: Derived from Natural Gas Prices, EIA Website; and Annual Energy Outlook, 2009 (April Revision), EIA/DOE..

October 8, 2010 MathPro
Single Octane NCG

Exhibit A-23: Average Price of Electricity to

Industrial Users, by Region

(¢/kwh)

Projected

Region 2007 2008 20151

PADD 1 8.19 9.16 7.80

PADD 2 5.63 6.28 5.35

PADD 3 7.23 7.84 6.67

PADD 4 4.93 5.17 4.40

PADD 5 9.13 9.96 8.48

California 9.52 9.54 8.12

U.S. 7.25 7.92 6.74

Note: Regional averages are calculated by weighting state prices by the

 distribution of crude oil distillation capacity.

1 Projected U.S. price is based on AEO 2009's projected price of electrcity

 to industrial users times the ratio of the 2007 price in the above table to

 the 2007 price reported in AEO 2009 . Regional projected prices are

 based on the projected U.S. price and regional to national price ratios in 2008.

Source: Derived from Table 5.6B, Electric Power Monthly , EIA/DOE.

 Annual Energy Outlook 2009 (April Revision) , EIA/DOE.

October 8, 2010 MathPro
Single Octane NCG

Exhibit B-1: Petroleum Supply and Disposition -- Historical 2003-2007 and

AEO 2009 Reference Case Forecast for 2015

(K b/d, except as noted)

Petroleum Supply. AEO Projected Growth

Disposition & Prices and Historical Forecast 2007-2015

Refining Capacity 2003 2004 2005 2006 2007 2015 Cumulative Annual

Supply

Crude Oil 15,340 15,529 15,284 15,195 15,071 13,924 -7.6% -1.0%

Domestic 5,690 5,468 5,191 5,102 5,067 5,420 7.0% 0.8%

 Alaska 990 910 864 741 719 508 -29.4% -4.3%

 Lower 48 4,710 4,558 4,327 4,361 4,348 4,912 13.0% 1.5%

Net Imports 9,650 10,061 10,093 10,093 10,004 8,505 -15.0% -2.0%

Natural Gas Plant Liquids 1,720 1,809 1,717 1,738 1,783 1,782 0.0% 0.0%

Net Product Imports 1,640 2,098 2,476 2,368 2,109 1,659 -21.3% -3.0%

Imports 2,600 3,057 3,577 3,583 3,430 2,916 -15.0% -2.0%

 Gross Refined Products2 1,850 2,069 2,449 2,171 1,938 1,528 -21.1% -2.9%

 Unfinished Oils 340 490 582 689 717 725 1.0% 0.1%

 Ethers

 Ethanol 10 6 46 22 2 -91.1% -26.1%

 Biodiesel

 Gasoline Blending Components3 410 488 540 677 753 661 -12.2% -1.6%

Exports 960 959 1,071 1,215 1,321 1,257 -4.8% -0.6%

Other Inputs1 440 341 396 363 721 1,489 106.5% 9.5%

Domestic Ethanol Production 221 255 319 425 957 125.2% 10.7%

Domestic Biodiesel Production 6 16 32 112 249.8% 16.9%

Liquids from Gas - - 

Liquids from Coal 74 - - 

Liquids from Biomass 11 - - 

Other 120 141 27 264 336 27.0% 3.0%

Disposition

Refined Products Supplied 20,060 20,760 20,798 20,655 20,650 20,021 -3.0% -0.4%

LPG 2,074 2,132 2,030 2,052 2,085 1,860 -10.8% -1.4%

E85 0 0 1 1 1 53 na na 

Motor Gasoline4 8,940 9,105 9,159 9,253 9,286 9,342 0.6% 0.1%

Jet Fuel 1,580 1,630 1,679 1,633 1,622 1,475 -9.1% -1.2%

Distillate Fuel & Kerosene 3,930 4,058 4,118 4,169 4,196 4,339 3.4% 0.4%

 Diesel Fuel 3,043 3,210 3,467 3,763 8.5% 1.0%

 Other 1,075 959 729 576 -21.0% -2.9%

Residual Oil 770 865 920 689 723 686 -5.1% -0.7%

Other5 2,766 2,970 2,891 2,858 2,737 2,267 -17.2% -2.3%

Energy Prices ($2007)

Crude Oil ($/b)

 Imported Low Sulfur Light Crudes6 46.95 61.94 69.65 72.33 103.87

 All Imported Crudes 32.73 40.61 53.57 62.33 63.83 96.77

Natural Gas ($/mcf)

 Lower 48 Wellhead 5.84 6.35 8.34 6.66 6.22 5.45

 Industrial End-Use 6.64 7.52 9.42 8.40 7.73 6.51

Electricity, Industrial End-Use (¢/Kwh) 6.10 5.93 6.26 6.45 6.35 5.91

LPG, Industrial End-Use (¢/g) 160.6 185.5 199.9 220.1

Domestic Refining

Crude Distillation Capacity (K b/d) 16,800 16,947 17,126 17,339 17,441 18,219

Capacity Utilization (%) 93.0 93.0 91.0 90.0 89.0 78.0

Note: Projected growth rates are calculated using 2004 as the base year because of the impact of hurricane Katrina in 2005.

1 Includes alcohols, ethers, petroleum product stock withdrawals, domestic sources of blending components, other hydrocarbons,

 and coal and natural gas converted to liquid fuel.

2 Includes non-ether, gasoline blending components for 1999-2001.

3 Includes imports of ethers in 2002 and thereafter.

4 Includes ethanol and ethers blended into gasoline.

5 Includes aviation gasoline, petrochemical feedstocks, lubricants, waxes, asphalt, road oil, still gas, special naphthas

 petroleum coke, crude oil product supplied, and miscellaneous petroleum products.

6 The projected price for imported low sulfur light crudes is adjusted upwards based on the historical relationship between WTI and Imported crudes.

Source: Derived from Year-by-Year Tables 1, 8, 11, 12, & 13, Annual Energy Outlook 2009 (April Revision), EIA/DOE;

 and Tables A11, A13, & A14; Annual Energy Outlook 2008 (and previous), EIA/DOE. 

October 8, 2010 MathPro
Single Octane NCG

Exhibit B-2: U.S. Imports and Exports of Petroleum Products --

Reported 2003-2008 and Projected 2015

(K b/d)

Historical Projected

Commodity 2003 2004 2005 2006 2007 2008 2015

IMPORTS 2,599 3,058 3,551 3,537 3,408 3,105 2,916

Gross Refined Products 1,853 2,075 2,449 2,170 1,939 1,549 1,528

Natural Gas Liquids 271 306 374 360 276 275 304

 Pentanes Plus 46 43 47 27 29 22 26

 Liquefied Petroleum Gases 225 264 328 332 247 254 278

Finished Motor Gasoline 518 498 603 475 413 302 0

 Reformulated 249 213 239 53 0 0 0

 Other 269 285 364 422 413 302 0

Jet Fuel (incl. Kerosene, & Aviation Gas) 115 130 199 191 220 105 100

Distillate Fuel Oil 333 326 329 365 304 214 419

 15 ppm or less sulfur 4 112 175 121 314

 15 to 500 ppm sulfur 135 149 152 77 13 17 0

 > 500 ppm sulfur 198 178 173 176 116 76 105

Naphthas (for Petrochemical) 87 134 151 132 94 92 106

Other Oils (Petrochemical) 146 158 159 174 150 125 150

Special Naphthas 11 8 14 15 17 16 16

Residual Oil 327 427 530 350 372 350 357

 < 0.31 wt% Sulfur 50 89 93 32 46 18 32

 0.31 to 1.00 wt% Sulfur 100 141 175 79 89 62 76

 > 1.00 wt% Sulfur 178 198 262 240 237 270 249

Asphalt & Road Oil 12 43 43 50 40 25 25

Lubricants & Waxes 8 12 15 19 20 23 21

Miscellaneous Products 100000 0

Petroleum Coke 22 33 32 40 32 22 31

Unfinished Oils 335 491 582 689 717 765 725

Ethanol 1 10 40 48 29 35 2

Ethers 44 39 9 8 0 0 - 

Gasoline Blending Components 367 452 510 669 753 791 661

Reformulated 90 228 318 286 239

Conventional 420 441 435 505 423

EXPORTS 1,014 1,024 1,133 1,292 1,405 1,778 1,257

Finished Petroleum Products 897 916 1,010 1,144 1,247 1,612 1,100

Finished Motor Gasoline 125 125 136 142 127 172 102

Special Naphthas 22 27 21 14 18 13 8

Jet Fuel , Kerosene, & Aviation Gas 28 44 55 44 50 67 39

Distillate Fuel Oil 107 110 138 215 268 530 314

 15 ppm or less sulfur 0 0 0000 0

 15 to 500 ppm sulfur 50 33 39 64 176 456 270

 > 500 ppm sulfur 57 77 99 151 91 73 43

Residual Fuel Oil 197 205 251 283 330 356 211

Asphalt & Road Oil 10 6 11 15 19 23 14

Lubricants & Waxes 41 45 45 59 64 65 39

Miscellaneous Products 636767 4

Petroleum Coke 361 351 347 366 366 378 370

Natural Gas Liquids 59 46 60 68 70 101 80

Other Liquids 59 63 64 80 88 64 77

Other Hydrocarbons/H2/Oxygenates 29 30 42 72 71 47 63

Motor Gasoline Blending Components 30 33 22 8 17 17 14

October 8, 2010 Page 1 of 2 MathPro
Single Octane NCG

Exhibit B-2: U.S. Imports and Exports of Petroleum Products --

Reported 2003-2008 and Projected 2015

(K b/d)

Notes on derivation of projections:

IMPORTS -- EIA projection of net product imports plus exports from Exhibit B-1.

Gross Refined Products -- EIA projection from Table B-1

 Natural Gas Liquids -- sum of projected pentanes and LPG

 Pentanes Plus -- average of imports from 2006 to 2008

 Liquified Petroleum Gases -- average of imports from 2006 to 2008

 Finished Motor Gasoline -- assumed no imports of finished gasoline

 Jet Fuel -- set at 100 K b/d (projected use of jet fuel in 2015 is about 150 K b/d lower than in 2008

 Distillate Fuel Oil -- projected gross refined imports less projected import volumes of all other refined products

 Distillate Fuel Oil <= 15 pmm -- assumed to be 75% of total diesel fuel imports with advent of low sulfur diesel standard

 Distillate Fuel Oil 15 to 500 pmm -- assumed to be zero

 Distillate Fuel Oil > 500 ppm -- difference between projected total distillate fuel imports and imports of ultra low sulfur diesel

 Naphthas (for Petrochemcial) -- average of imports from 2006 to 2008

 Other Oils (Petrochemical) -- average of imports from 2006 to 2008

 Special Naphthas -- average of imports from 2006 to 2008

 Residual Oil Total -- average of imports from 2006 to 2008

 Residual Oil by Sulfur Content -- total imports times pro rata share over last three years

 Asphalt & Road Oil -- average of imports from 2006 to 2008

 Lubricants & Waxes -- average of imports from 2006 to 2008

 Petroleum Coke -- average of imports from 2006 to 2008

Unfinished Oils -- EIA projection from Table B-1

Ethanol -- EIA projection from Table B-1

Ethers -- assumed to be zero

Gasoline Blending Components -- EIA projection from Table B-1

 Reformulated/conventional volumes based on shares in 2008

EXPORTS -- EIA projection from Table B-1

Finished Petroleum Products:

 Total -- difference between DOE projection of total exports and projected exports of NGL and other liquids

 Specific Finished Products -- share of finished products less coke in 2008 times the projected finished products less coke

 Petroleum coke -- average of exports from 2006 to 2008

Natural Gas Liquids -- average of exports from 2006 to 2008

Other Liquids -- average of exports from 2006 to 2008

Sources: Derived from Tables 20 & 27 (2000-2004) and Tables 23 & 29 (2005-2008), Petroleum Supply Annuals, EIA/DOE.

 DOE Refinery-Level Import Data (for ethanol imports, 2003-2005); and Exhibit B-1.

October 8, 2010 Page 2 of 2 MathPro
Single Octane NCG

Exhibit B-3: Projected Growth in Volume of Refined Product

Consumption, by Region

2007 to 2015

Region

Petroleum PADD P4&5 ex

Product 1 2 3 CA2 Calif. Total

Motor Gasoline & E85 0.3% -1.3% 3.9% 8.1% 1.7% 0.6%

Jet & Kerosene -9.0% -11.0% -8.0% -7.5% -8.7% -9.1%

Distillate 0.4% 3.1% 6.1% 6.9% 5.6% 3.4%

Residual Oil -3.1% -46.1% -6.2% 1.8% 8.3% -5.1%

Petro Feedstock -17.2% -16.6% -17.3% -17.2% -17.2% -17.1%

Lubes & Wax -25.0% -2.8% -19.3% 11.0% 21.6% -12.4%

Asphalt -28.6% -7.5% -23.2% 5.6% 15.7% -12.4%

Sources: Derived from Table 11 and Supplement Tables 1-10, Annual Energy Outlook 2009 (April Revision), DOE/IEA; 

 Tables 48, 49, & 50 (Prime Supplier Sales), Petroleum Marketing Annual 2007 , EIA/DOE;

 Table M21, Federal Highway Statistics 2007 , FHWA;

October 8, 2010 MathPro
Single Octane NCG

Exhibit B-4: Projected Annual Supply of Major Refined Products,

by Region -- 2015

(K b/d)

PADD PDs 4&5 U.S.

Product/Source 1 2 3 ex Calif1 Calif. Total

Gasoline & E852 3,341 2,579 1,467 974 1,034 9,395

E85 15 23 10 0 5 53

Gasoline 3,326 2,556 1,457 974 1,029 9,342

Refinery & Blender Production3 3,326 2,556 1,558 974 1,029 9,444

 Net Blndstk Purchases4 2,231 530 -2,346 259 -25 647

 Net Imports 586 0 0 0 62 647

 Net Inter-PADD Shipments 1,645 530 -2,346 164 7

 From Puget Sound 0 0 0 -57 57

 From California 0 0 0 175 -175

 Production - Blndstk Pur5 847 1,968 4,165 686 1,058 8,724

Net Imports 0 0 -102 0 0 -102

RFG 1,447 483 350 80 1,029 3,389

Refinery & Blender Production3 1,447 483 350 80 1,029 3,389

 Net Blndstk Purchases 4 684 99 -596 36 16 239

 Net Imports 235 0 0 0 4 239

 Net Inter-PADD Shipments 449 99 -596 48 0 0

 From Puget Sound 0 0 0 -57 57 0

 From California 0 0 0 46 -46 0

 Production - Blndstk Pur 5 687 373 1,012 40 1,012 3,123

Net Imports 0 0 0 0 0 0

CG 1,879 2,073 1,107 894 0 5,953

Refinery & Blender Production3 1,879 2,073 1,209 894 0 6,055

 Net Blndstk Purchases 4 1,547 431 -1,750 222 -41 409

 Net Imports 351 0 0 0 58 409

 Net Inter-PADD Shipments 1,196 431 -1,750 116 7 0

 From Puget Sound 0 0 0 0 0 0

 From California 0 0 0 130 -130 0

 Production - Blndstk Pur 5 160 1,594 3,154 647 46 5,601

Net Imports 0 0 -102 0 0 -102

Distillate & Resid

Jet Fuel & Kerosene 586 276 122 280 240 1,504

Refinery Production 87 192 736 195 234 1,444

Net Imports 33 -2 -6 6 30 61

Net Inter-PADD Shipments 466 87 -607 55

Net shipments from CA 24 -24

Diesel Fuel Oil 1,356 1,304 851 504 295 4,310

Refinery Production 495 928 2,072 356 354 4,205

Net Imports 191 36 -166 0 45 105

Net Inter-PADD Shipments 671 339 -1,054 44 1

Net shipments from CA 104 -104

Residual Oil 323 23 159 61 119 686

Refinery Production 121 33 208 108 70 540

Net Imports 172 0 -28 -36 38 146

Net Inter-PADD Shipments 30 -10 -20 0 0

Net shipments within P4&5 -11 11

October 8, 2010 Page 1 of 2 MathPro
Single Octane NCG

Exhibit B-4: Projected Annual Supply of Major Refined Products,

by Region -- 2015

(K b/d)

PADD PDs 4&5 U.S.

Product/Source 1 2 3 ex Calif1 Calif. Total

Other Products

Petrochemical Fdstk. 22 40 462 2 6 533

Refinery Production 18 39 212 2 6 277

Net Imports 4 0 251 0 0 256

Net Inter-PADD Shipments 0 1 -1 0 0

Lubes & Waxes 23 30 58 -3 20 129

Refinery Production 18 17 91 0 20 147

Net Imports -2 -2 -13 -2 0 -18

Net Inter-PADD Shipments 7 15 -20 -1 0

Asphalt & Road Oil 93 161 56 62 45 418

Refinery Production 71 162 70 58 45 407

Net Imports 11 0 -4 4 0 11

Net Inter-PADD Shipments 11 -1 -10 0 0

Note: Increases in stocks are included in total product supplied and vice versa.

1 Includes refined products supplied by California refineries.

2 Finished gasoline and E85 consumed in the PADD.

3 Finished gasoline produced by refineries and by within-PADD blenders; includes 10% ethanol.

4 Gasoline blendstocks, RBOB, CBOB, and GTAB ex ethanol

5 Finished gasoline made from refinery-produced gasoline blendstocks; includes 10% ethanol.

Source: Derived from Exhibits A-2, B-1, B-2, and B-3.

October 8, 2010 Page 2 of 2 MathPro
Single Octane NCG

Exhibit B-5: Projected Annual Refinery Inputs & Outputs, 2015

(K b/d)

Inputs & Outputs PADD 1 PADD 2 PADD 3 P45 ex CA CA US

Inputs1 1,760 3,576 8,249 1,489 1,939 17,013

Crude Oil 1,477 3,204 7,135 1,411 1,735 14,961

Natural Gas Liquids and LPG 17 96 251 59 7 430

Pentanes Plus 0 51 99 4 21 175

Liquified Petroleum Gases 17 45 152 56 -14 255

 Normal Butane-Butylene 5 0 45 24 -14 60

 Isobutane-Isobutylene 12 44 107 32 0 195

Other Liquids 267 276 863 19 196 1,621

Fuel Ethanol 96 213 424 69 109 911

Unfinished Oils 171 63 439 -45 72 701

 Naphtha and Lighter 32 19 26 -3 -16 58

 Kerosene and Light Oils -7 23 -33 -3 -12 -34

 Heavy Gas Oils 59 41 370 -33 93 531

 Residuum 87 -21 77 -5 7 146

Gasoline Blending Components 0 0 0 -5 15 10

Outputs 1,728 3,490 8,002 1,432 1,845 16,498

Liquified Petroleum Gases 52 110 368 23 39 593

Ethane-Ethylene 0 0 20 0 0 20

Propane/Propylene 52 110 348 23 39 573

 Propane

 Propylene

Normal Butane-Butylene 000000

 Normal Butane

 Normal Butylene

Isobutane-Isobutylene 000000

 Isobutane

 Isobutylene

Finished Refined Products2 1,676 3,380 7,634 1,409 1,806 15,905

E85 15 23 10 0 5 53

Finished Motor Gasoline3 847 1,968 4,165 686 1,058 8,724

 Reformulated 687 373 1,012 40 1,012 3,123

 Conventional 160 1,594 3,154 647 46 5,601

Aviation Gasoline 0 3 11 2 0 16

Jet Fuel & Kerosene 87 192 736 195 234 1,444

Distillate 495 928 2,072 356 354 4,205

 0-15 ppm Sulfur 300 913 2,015 349 104 3,681

 15-500 ppm Sulfur 0 0

 > 500 ppm Sulfur 195 15 57 7 0 275

 CARB Diesel 250 250

Residual Fuel Oil 121 33 208 108 70 540

 0-0.3 Sulfur 40 0 21 6 3 70

 0.31-1.0 Sulfur 55 3 16 31 20 126

 Greater Than 1% Sulfur 26 30 171 71 46 344

Pet Chem Feedstocks 18 39 212 2 6 277

 Naphtha 18 31 96 0 0 145

 Other Oils 0 8 116 2 6 132

Special Naphtha 0 4 27 1 0 33

Lubes & Waxes 18 17 91 0 20 147

Asphalt and Road Oil 71 162 70 58 45 407

Miscellaneous (nonfuel use) 2 11 31 0 14 60

1 Excludes hydrogen purchases.

2 Excludes petroleum coke, still gas, and miscellaneous fuel use

3 Includes RBOB and CBOB volumes and associated oxygenate volumes.

Sources: Derived from Exhibits A-3 and B-4

October 8, 2010 MathPro
Single Octane NCG

Exhibit B-6: Projected Seasonal Refinery Inputs & Outputs, 2015

(K b/d)

PADD 1 PADD 2 PADD 3 PADD 45 ex CA CA 

Inputs & Outputs Summer Winter Summer Winter Summer Winter Summer Winter Summer Win

Inputs1 1,780 1,761 3,664 3,562 8,300 8,235 1,497 1,475 1,969 

Crude Oil 1488 1466 3267 3141 7246 7024 1449 1372 1698 Natural Gas Liquids and LPG 14 39 109 156 213 326 35 79 21 Pentanes Plus 62 40 99 99 2 5 20 Liquified Petroleum Gases 14 39 48 116 114 227 33 74 2 

 Normal Butane-Butylene 0 26 0 71 0 119 0 44 0  Isobutane-Isobutylene 14 13 48 46 114 109 33 30 2 

Other Liquids 278 256 288 264 842 885 14 24 250 Fuel Ethanol 95 96 213 214 420 428 68 69 110 Unfinished Oils 183 160 75 50 422 457 -49 -40 125 

 Naphtha and Lighter 34 21 20 21 33 26 -4 -1 -12 

 Kerosene and Light Oils -8 -10 30 14 -33 11 -5 -15 -24  Heavy Gas Oils 58 74 43 37 362 355 -33 -26 153  Residuum 100 74 -18 -21 60 66 -7 1 8 

Gasoline Blending Components -5 -5 15 

October 8, 2010 Page 1 of 2 
Single Octane NCG

Exhibit B-6: Projected Seasonal Refinery Inputs & Outputs, 2015

(K b/d)

PADD 1 PADD 2 PADD 3 PADD 45 ex CA CA 

Inputs & Outputs Summer Winter Summer Winter Summer Winter Summer Winter Summer Win

Outputs 1,741 1,738 3,552 3,497 7,995 8,037 1,438 1,426 1,835 Liquified Petroleum Gases 73 54 181 109 406 359 22 25 40 Ethane-Ethylene 0 0 0 0 20 20 Propane/Propylene 52 52 112 109 347 349 22 24 40 

 Propane 32 31 87 89 169 159 0 0 0  Propylene 20 20 25 19 178 191 22 24 40 

Normal Butane-Butylene 19 0 68 1 38 -10 0 0 0 

 Normal Butane 19 0 65 0 41 0 0 0 0  Normal Butylene 0 0 3 1 -3 -10 0 0 0 

Isobutane-Isobutylene 210000000

 Isobutane 000000000 Isobutylene 210000000

Finished Refined Products2 1,668 1,684 3,372 3,388 7,589 7,678 1,417 1,401 1,795 

E85 15 15 23 23 10 10 0 0 5 Finished Motor Gasoline3 841 853 1964 1971 4124 4206 678 694 1066 

 Reformulated 697 677 366 380 994 1029 29 50 1005  Conventional 144 177 1598 1591 3130 3177 649 644 62 

Aviation Gasoline 3 3 12 10 2 2 Jet Fuel & Kerosene 85 90 190 194 733 738 201 189 220 Distillate 493 497 923 933 2057 2086 365 348 350 

 0-15 ppm Sulfur 310 289 909 916 1993 2037 357 342 101  15-500 ppm Sulfur  > 500 ppm Sulfur 183 208 15 16 65 49 8 6 0  CARB Diesel 249 

Residual Fuel Oil 125 117 33 32 217 199 107 109 63 

 0-0.3 Sulfur 39 48 0 0 21 19 89 82 0  0.31-1.0 Sulfur 59 40 3 4 16 19 44 38 0  Greater Than 1% Sulfur 26 29 30 29 179 162 66 70 0 

Pet Chem Feedstocks 19 17 41 37 216 208 3 1 9 

 Naphtha 19 17 32 30 99 90 1 1 0  Other Oils 0 0 9 8 117 118 4 1 0 

Special Naphtha 0 0 5 4 24 31 1 1 Lubes & Waxes 18 18 18 16 93 89 0 0 21 Asphalt and Road Oil 69 74 161 163 71 69 60 57 47 Miscellaneous (nonfuel use) 2 2 11 11 31 31 0 0 14 

1 Excludes hydrogen purchases.2 Excludes petroleum coke, still gas, and miscellaneous fuel use3 Includes RBOB and CBOB volumes and associated ethanol volumes.Sources: Derived from Exhibits A-4 and B-5.

October 8, 2010 Page 2 of 2 
Single Octane NCG

Exhibit B-7: Projected Distribution of Summer Conventional and

Low-RVP Gasoline, and Gasoline Pool RVP Projected

Under the 8-Hour Ozone Standard, 2015

Gasline Distribution (%) Average Pool RVP (psi)

Conven- Low RVP 8-Hour

Region tional 7.8 7.01 Total Ozone Std. NCG

Within Region Use 57% 35% 9% 100%

PADD 1 48% 43% 9% 100%

Subdistrict 1A 62% 38% 100%

Subdistrict 1B 21% 79% 100%

Subdistrict 1C 56% 32% 12% 100%

PADD 2 63% 24% 14% 100%

PADD 3 60% 34% 6% 100%

PADDs 4 & 5 ex CA 56% 44% 100%

California 0%

Refinery Production 57% 35% 9% 100%

PADD 1 34% 66% 100% 8.7 7.1

PADD 2 66% 26% 8% 100% 9.1 7.5

PADD 3 54% 33% 12% 100% 8.9 7.3

PADDs 4 & 5 ex CA 52% 48% 100% 8.9 7.3

California 11% 89% 100% 8.3 6.9

Note: For the 8-Hour Ozone standard, average pool RVP reflects the effects of the 1 psi ethanol RVP waiver, except for 

 low-RVP gasoline during July and August. For NCG, the 1 psi ethanol waiver applies only to conventional gasoline.

Source: Derived from Exhibit A-15 and Exhibit B-6c, "Refining Economcs of a National Clean Gasoline

 Gasoline Standard for PADDs 1-3," for The Alliance of Automobile Manufactureres,

 MathPro Inc., 05/07/07.

October 8, 2010 MathPro
Single Octane NCG

Exhibit B-8: Projected Distribution of Refining Regions' Gasoline Production,

Grade Splits, and Pool Octane, by PADD -- 2015

Pool

Supplying Share of Production Shipped To: Premium Octane

Region PADD 1 PADD 2 PADD 3 PADD 4 PADD 5 Grade Split (R+M)/2

PADD 1Reformulated 100.0% 12.9% 88.3All Other 100.0% 9.0% 88.0PADD 2Reformulated 97.4% 2.6% 10.4% 88.3All Other 0.9% 95.6% 1.8% 1.6% 9.1% 88.0PADD 3Reformulated 34.1% 12.6% 40.1% 13.1% 11.6% 88.1All Other 48.6% 13.7% 34.8% 1.5% 1.5% 9.1% 88.0PADD 4-5 ex CA

ReformulatedAll Other 7.0% 84.4% 8.7% 12.5% 87.4CaliforniaCARBOB1 100.0% 15.7% 84.5

Reformulated 100.0% 15.7% 88.0All Other 100.0% 11.1% 87.9

1 With 10% ethanol blending.Note: The premium grade split includes 40% of the mid-grade share. Premium shares for conventional gasoline reflect resumption of shipments of premium from PADD 3 to PADD 2Source: Derived from Exhibit A-16b.

October 8, 2010 
Single Octane NCG

Exhibit C-1: Estimated Effects of NCG and Single Octane NCG Standards on Cost and

on Crude Oil Use, Energy Use, and CO2 Emissions

PADD 1 PADD 2 PADD 3 PADDs 1-3 

Single Octane Single Octane Single Octane Single O

94 RON 95 RON 94 RON 95 RON 94 RON 95 RON 94 RON 

NCG NCG NCG NCG NCG NCG NCG NCG NCG NCG NCG 

Effects on Costs

Refining CostTotal ($B/y) 0.5 0.8 1.1 0.9 1.8 2.6 1.9 3.9 6.1 3.4 6.4 

 Capital charge & fixed cost 0.3 0.3 0.5 0.4 0.4 0.5 0.6 0.7 1.0 1.2 1.4  Reduction in Cash Flow 1 0.3 0.5 0.7 0.5 1.4 2.2 1.4 3.2 5.1 2.1 5.1 

Per Gallon of Gasoline (¢/gal) 4.2 5.8 8.8 3.0 6.0 8.8 3.0 5.9 9.4 3.1 5.9 Value of Improved GasolineEnergy Density (¢/gal)$B/y 0.0 0.1 0.1 0.2 0.5 0.7 0.5 0.7 1.4 0.7 1.2 Per Gallon of Gasoline (¢/gal) 0.1 0.5 0.7 0.7 1.7 2.3 0.8 1.0 2.2 0.7 1.1 Refinery Investment ($B) 1.0 1.0 1.7 1.3 1.3 1.7 2.0 2.4 3.5 4.3 4.7 

Costs Associated with

Retrofitting to 5 ppm Sulfur2Investment ($B) 0.6 0.7 0.6 0.8 0.9 0.9 2.1 2.0 2.0 3.5 3.5 Capital charge & fixed cost ($B/y) 0.2 0.2 0.2 0.2 0.2 0.3 0.6 0.6 0.6 1.0 1.0 Per Gallon of Gasoline (¢/gal) 1.4 1.5 1.5 0.8 0.8 0.8 0.9 0.9 0.9 1.0 1.0 Effects on OperationsChange in Crude Oil Inputper Barrel of Gasoline (b/b) 0.01 0.02 0.03 0.01 0.03 0.05 0.01 0.03 0.04 0.01 0.03 

Changes in Energy Use (Fuel & Power)

Total (Trillion btu/y) 13.4 19.0 25.2 18.2 32.4 45.4 33.9 70.9 121.7 65.5 122.2 Percent Increase 5% 7% 10% 3% 6% 8% 2% 5% 8% 3% 5% Changes in CO2 EmissionsTotal (Million MT/y) 0.9 1.1 1.4 1.1 1.7 2.4 2.1 3.7 6.1 4.0 6.6 Percent Increase 4% 6% 7% 2% 4% 5% 2% 3% 5% 2% 4% 

1 Cash Flow is defined here as refinery revenues (from the sale of refined products) less all direct (non-investment related) costs, such as purchases of crude oil, unfinished oils, gasoline blendstocks, natural gas, electricty, and catalysts.2 The indicated refining costs include the cost of retrofitting for desulfurization of FCC naphtha to 5 ppm for all FCC naphtha post-treaters. Estimated costs would be lower if some portion of these units already could produce 5 ppm FCC naphtha.

October 8, 2010 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

USE OF IN-PLACE CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackingCoking

Upgrading Alkylation*

Iso-octene/octaneCatalytic Polymerization*Dimersol*Pen/Hex IsomerizationReforming

Hydrotreating Naphtha Desulf.

FCC Naphtha DesulfurizationBenzene SaturationDistillate DesulfurizationDistillate DearomatizationFCC Feed Desulfurization

Hydrogen Hydrogen* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Med. Naphtha Spl.Hvy. Reformate Spl.FCC Naphtha SplittingHeavy FCC/Lt Cycle Oil Splitting

Other Butane Isomerization

Aromatics RecoveryBenzene ExtractionLubes & Waxes*Sulfur Recovery* (K s tons/d)Steam Generation (K lb/hr)

Refinery Modeling Results -- Refinery Operations and New CaPADD 1(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

1,498 1,478 1,455 1,427 1,465 1,432 1,477 1,4

546 546 546 524 529 540 546 5

22 23 22 23 22 21 22 82 82 82 83 82 86 82 97 76 97 78 97 81 97 18 15 17 15 12 15 13 17 17 17 17 17 17 17 

257 220 219 172 245 196 274 2330 293 315 273 340 296 348 2349 349 349 336 346 349 349 3

10 6 10 12 10 16 10 

393 398 438 414 450 418 442 4

43 42 44 40 43 42 44 

104 113 113 157 113 170 113 1102 62 102 58 102 53 102 

64 69 63 69 69 56 64 

25 

38 12 38 16 38 38 38 20 17 25 20 25 21 27 18 17 18 18 18 18 18 

1111111

3,501 3,138 3,474 3,072 3,378 3,228 3,593 3,3

October 8, 2010 Page 1 of 8 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

NEW CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackerCoker

Upgrading Alkylation*

Pen/Hex IsomerizationReforming

Hydrotreating FCC Naphtha Desulfurization

Benzene SaturationDistillate DesulfurizationFCC Feed Desulfurization

Hydrogen Hydrogen Plant* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Medium Naphtha Spl. Hvy. Reformate Spl.FCC/Lt Cycle Oil Splitting

Other Aromatics Recovery

Benzene ExtractionLube Oil Production

Retrofitting Tier 2 Diesel Desulfurization

Ultra Low Sulfur Gasoline

OPERATIONSFluid Cat Cracker Charge Rate

Conversion (Vol %)Olefin Max Cat. (%)Catalyst Coke (K b/d)

Hydrocracker Charge Rate: Gas Oils

 All OtherNaphtha as % of Out-turns (%)Kero & Dist. as % of Out-turns (%)

Reformer Charge Rate

Severity (RON)

Fuel Use Natural Gas & Refinery Gases (foebEnergy Use Fuel & Power (Billion btu/d)CO2 Emissions CO2 Emissions (K MT/d)

* Capacity defined in terms of volume of output.

Refinery Modeling Results -- Refinery Operations and New CaPADD 1(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

18 24 24 

3 

5 5588

49 64 41 

2222 2 35 

27 312 73 2

588

38 38 37 

73 10 0 0 346 349 353 3

675 665 691 642 680 660 692 6

68.2 70.2 66.9 69.9 66.1 70.1 66.8 7

3.0 4.8 4.6 5.0 

30 31 29 29 29 30 30 20 23 20 23 21 22 21 

9898878

55.8 49.5 52.1 47.2 60.1 46.9 56.9 445.3 24.4 37.6 32.2 38.2 17.5 50.0 1

247 215 235 190 258 219 266 2

100.6 100.1 96.0 94.8 96.9 94.2 100.1 9

71 66 70 64 74 70 77 

727 695 720 672 748 718 767 7

54 52 54 51 56 54 57 

October 8, 2010 Page 2 of 8 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

USE OF IN-PLACE CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackingCoking

Upgrading Alkylation*

Iso-octene/octaneCatalytic Polymerization*Dimersol*Pen/Hex IsomerizationReforming

Hydrotreating Naphtha Desulf.

FCC Naphtha DesulfurizationBenzene SaturationDistillate DesulfurizationDistillate DearomatizationFCC Feed Desulfurization

Hydrogen Hydrogen* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Med. Naphtha Spl.Hvy. Reformate Spl.FCC Naphtha SplittingHeavy FCC/Lt Cycle Oil Splitting

Other Butane Isomerization

Aromatics RecoveryBenzene ExtractionLubes & Waxes*Sulfur Recovery* (K s tons/d)Steam Generation (K lb/hr)

Refinery Modeling Results -- Refinery Operations and New CaPADD 2(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

3,249 3,111 3,193 3,058 3,240 3,059 3,294 3,01,068 890 1,042 890 1,021 890 1,046 8

188 185 188 185 188 185 188 1301 308 301 311 301 311 301 3246 180 246 205 246 208 246 2

5353535333 3 3

173 173 173 148 173 142 173 1737 658 586 510 656 511 763 6825 772 852 750 936 750 951 7609 518 600 507 593 507 607 5

6 6 35 6 36 6 

1,032 1,049 1,049 1,049 1,018 1,049 1,027 1,0

474 441 478 433 475 433 484 4712 799 799 826 799 813 785 7232 106 232 101 232 96 232 1193 251 228 251 251 257 251 2

24 24 15 24 24 24 29 29 35 28 50 27 50 16 15 17 16 17 16 17 

4444444

6,413 5,457 6,797 5,452 7,150 5,394 7,237 5,6

October 8, 2010 Page 3 of 8 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

NEW CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackerCoker

Upgrading Alkylation*

Pen/Hex IsomerizationReforming

Hydrotreating FCC Naphtha Desulfurization

Benzene SaturationDistillate DesulfurizationFCC Feed Desulfurization

Hydrogen Hydrogen Plant* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Medium Naphtha Spl. Hvy. Reformate Spl.FCC/Lt Cycle Oil Splitting

Other Aromatics Recovery

Benzene ExtractionLube Oil Production

Retrofitting Tier 2 Diesel Desulfurization

Ultra Low Sulfur Gasoline

OPERATIONSFluid Cat Cracker Charge Rate

Conversion (Vol %)Olefin Max Cat. (%)Catalyst Coke (K b/d)

Hydrocracker Charge Rate: Gas Oils

 All OtherNaphtha as % of Out-turns (%)Kero & Dist. as % of Out-turns (%)

Reformer Charge Rate

Severity (RON)

Fuel Use Natural Gas & Refinery Gases (foebEnergy Use Fuel & Power (Billion btu/d)CO2 Emissions CO2 Emissions (K MT/d)

* Capacity defined in terms of volume of output.

Refinery Modeling Results -- Refinery Operations and New CaPADD 2(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

37 46 55 51 49 55 30 96 17 146 

1 36 36 

20 215 192 

6 7

51 49 55 

111

67 49 69 46 78 

0 0 0 0 477 4

1,040 968 1,048 950 1,041 950 1,061 9

75.7 69.8 73.5 70.3 72.8 70.3 73.1 7

17.1 0.1 20.6 20.5 1

48 41 46 41 46 41 47 

193 216 170 212 193 212 194 2

65 38 88 42 65 42 64 

66.9 67.3 59.8 67.0 52.3 67.1 56.9 614.3 13.8 22.9 14.2 31.6 14.1 26.0 1

711 638 645 582 721 577 787 6

100.6 100.4 94.8 92.6 94.8 93.3 97.7 9

175 165 174 161 186 165 191 1

1,643 1,521 1,631 1,494 1,703 1,521 1,748 1,5

124 116 125 116 128 119 131 1

October 8, 2010 Page 4 of 8 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

USE OF IN-PLACE CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackingCoking

Upgrading Alkylation*

Iso-octene/octaneCatalytic Polymerization*Dimersol*Pen/Hex IsomerizationReforming

Hydrotreating Naphtha Desulf.

FCC Naphtha DesulfurizationBenzene SaturationDistillate DesulfurizationDistillate DearomatizationFCC Feed Desulfurization

Hydrogen Hydrogen* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Med. Naphtha Spl.Hvy. Reformate Spl.FCC Naphtha SplittingHeavy FCC/Lt Cycle Oil Splitting

Other Butane Isomerization

Aromatics RecoveryBenzene ExtractionLubes & Waxes*Sulfur Recovery* (K s tons/d)Steam Generation (K lb/hr)

Refinery Modeling Results -- Refinery Operations and New CaPADD 3(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

7,461 7,004 7,269 6,891 7,371 6,887 7,464 6,92,590 2,457 2,590 2,297 2,590 2,352 2,590 2,5

512 512 512 666 512 611 512 5

1,185 1,185 1,185 1,265 1,185 1,268 1,185 1,2

581 581 581 566 581 581 581 5

22 11 22 10 12 10 12 

838 8

235 235 235 235 235 235 235 4

1,500 1,160 1,149 1,005 1,285 997 1,488 1,11,674 1,583 1,664 1,585 1,742 1,584 1,885 1,61,494 1,423 1,494 1,339 1,494 1,372 1,494 1,4

5 5 5 5 5 5 5 

2,215 2,191 2,241 2,265 2,241 2,314 2,241 2,31,142 1,099 1,172 1,043 1,158 1,069 1,161 1,11,649 1,649 1,649 2,275 1,649 2,258 1,649 2,2

589 480 589 479 589 480 589 5175 186 186 378 186 482 186 4

322 117 188 208 2

107 107 107 107 153 129 155 142 157 149 152 1

16 12 16 12 16 12 16 

144 136 93 89 93 89 93 

12 12 13 12 13 12 13 

22,193 20,703 18,585 16,691 18,543 16,721 19,368 17,6

October 8, 2010 Page 5 of 8 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

NEW CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackerCoker

Upgrading Alkylation*

Pen/Hex IsomerizationReforming

Hydrotreating FCC Naphtha Desulfurization

Benzene SaturationDistillate DesulfurizationFCC Feed Desulfurization

Hydrogen Hydrogen Plant* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Medium Naphtha Spl. Hvy. Reformate Spl.FCC/Lt Cycle Oil Splitting

Other Aromatics Recovery

Benzene ExtractionLube Oil Production

Retrofitting Tier 2 Diesel Desulfurization

Ultra Low Sulfur Gasoline

OPERATIONSFluid Cat Cracker Charge Rate

Conversion (Vol %)Olefin Max Cat. (%)Catalyst Coke (K b/d)

Hydrocracker Charge Rate: Gas Oils

 All OtherNaphtha as % of Out-turns (%)Kero & Dist. as % of Out-turns (%)

Reformer Charge Rate

Severity (RON)

Fuel Use Natural Gas & Refinery Gases (foebEnergy Use Fuel & Power (Billion btu/d)CO2 Emissions CO2 Emissions (K MT/d)

* Capacity defined in terms of volume of output.

Refinery Modeling Results -- Refinery Operations and New CaPADD 3(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

171 110 30 127 142 167 

200 

30 38 1727 16 81 211 

231 232 929 236 909 285 676 

000

40 171 315 

213 84 369 330

94 187 1

464 30 511 448 

0 0 0 0 1,444 1,204 1,430 1,3

2,625 2,527 2,694 2,397 2,662 2,457 2,668 2,5

73.6 72.8 72.5 72.1 73.0 72.1 72.6 724.7 25.6 24.0 29.3 17.0 28.6 17.7 2

119 114 117 108 117 110 120 1389 342 475 545 520 485 478 3123 171 191 121 91 127 61 1

48.1 34.8 42.5 42.6 44.1 42.1 41.3 436.1 52.2 42.5 42.5 40.8 43.1 44.1 4

1,456 1,146 1,203 1,046 1,333 1,048 1,451 1,1100.5 100.0 97.3 97.5 97.7 96.8 100.3 10

452 417 434 407 452 415 463 4

4,168 3,891 4,064 3,804 4,177 3,877 4,267 3,9

317 299 322 304 328 309 331 3

October 8, 2010 Page 6 of 8 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

USE OF IN-PLACE CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackingCoking

Upgrading Alkylation*

Iso-octene/octaneCatalytic Polymerization*Dimersol*Pen/Hex IsomerizationReforming

Hydrotreating Naphtha Desulf.

FCC Naphtha DesulfurizationBenzene SaturationDistillate DesulfurizationDistillate DearomatizationFCC Feed Desulfurization

Hydrogen Hydrogen* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Med. Naphtha Spl.Hvy. Reformate Spl.FCC Naphtha SplittingHeavy FCC/Lt Cycle Oil Splitting

Other Butane Isomerization

Aromatics RecoveryBenzene ExtractionLubes & Waxes*Sulfur Recovery* (K s tons/d)Steam Generation (K lb/hr)

Refinery Modeling Results -- Refinery Operations and New CaCalifornia(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

1,683 1,771 1,555 1,581 1,553 1,582 1,594 1,5

606 557 534 499 531 499 566 5368 368 368 368 368 368 368 3426 422 405 402 405 402 410 3170 118 169 96 176 95 176 1

25 5 51

111 104 94 93 89 100 92 320 308 254 245 263 248 350 3361 376 322 328 321 328 328 3115 124 105 249 125 271 119 2

31 25 26 22 27 21 31 

359 345 330 352 329 332 339 3

46 65 65 65 65 65 65 

585 555 556 521 553 521 560 5

1,172 1,217 1,234 1,188 1,232 1,190 1,152 1,1

145 64 134 75 134 75 150 127 180 101 85 160 131 138 1114 104 91 90 90 92 60 

41 50 27 49 26 50 

4 38 38 34 17 6 

139 129 139 132 131 124 122 1114 32 6 2 3 

47 47 47 7 47 6 47 18 17 20 19 20 19 20 

3333333

2,487 1,808 1,930 1,356 1,989 1,379 2,393 2,0

October 8, 2010 Page 7 of 8 
Single Octane NCG

Exhibit C-2:

Type

of Process

Process Wt% Oxygen -->

NEW CAPACITYCrude Distillation AtmosphericConversion Fluid Cat Cracker

HydrocrackerCoker

Upgrading Alkylation*

Pen/Hex IsomerizationReforming

Hydrotreating FCC Naphtha Desulfurization

Benzene SaturationDistillate DesulfurizationFCC Feed Desulfurization

Hydrogen Hydrogen Plant* (MM scf/d)Fractionation Debutanization

DepentanizationLt. Naphtha Spl. (Benz. Prec.)Medium Naphtha Spl. Hvy. Reformate Spl.FCC/Lt Cycle Oil Splitting

Other Aromatics Recovery

Benzene ExtractionLube Oil Production

Retrofitting Tier 2 Diesel Desulfurization

Ultra Low Sulfur Gasoline

OPERATIONSFluid Cat Cracker Charge Rate

Conversion (Vol %)Olefin Max Cat. (%)Catalyst Coke (K b/d)

Hydrocracker Charge Rate: Gas Oils

 All OtherNaphtha as % of Out-turns (%)Kero & Dist. as % of Out-turns (%)

Reformer Charge Rate

Severity (RON)

Fuel Use Natural Gas & Refinery Gases (foebEnergy Use Fuel & Power (Billion btu/d)CO2 Emissions CO2 Emissions (K MT/d)

* Capacity defined in terms of volume of output.

Refinery Modeling Results -- Refinery Operations and New CaCalifornia(K b/d, except as noted)

2015

2007 Sing

Calibration Reference NCG 94 RON 

Sum Win Sum Win Sum Win Sum Win 

187 185 213 

11 11 

111

3 5 3 

152 158 167 158 192 1

585 555 556 521 553 521 560 5

78.7 76.1 73.0 72.7 72.8 72.7 76.7 7

0.9 3.0 

29 27 27 26 27 26 28 

260 281 258 260 258 260 262 2108 87 110 108 110 108 106 1

44.3 42.2 41.6 41.2 41.7 40.9 41.2 441.0 43.2 43.9 44.4 43.8 44.8 44.4 4

335 334 282 273 292 276 344 3

96.2 93.7 91.7 91.7 91.6 91.7 100.0 9

121 120 116 111 117 111 122 1

1,128 1,102 1,079 1,019 1,084 1,024 1,128 1,0

98 97 95 90 95 91 97 

October 8, 2010 Page 8 of 8 
Single Octane NCG

Exhibit C-3:

Inputs/

Outputs

Crude Oil

Other Inputs

Isobutane

Butane

Butylene

Natural Gas Liquids

Gasoline Blendstocks

Straight Run Naphtha

Kerosene

Heavy Gas Oil

Resid

Ethanol -- RFG

 All Other

Purchased Energy

Electricity (MM Kwh/d)

Natural Gas (K foeb/d)

Refined Products1

Aromatics

Ethane/Ethylene

Propane

Propylene

Butanes/Butylenes

Aviation Gas

Naphtha to PetroChem

Special Naphthas

Gasoline:

 CARBOB

 Federal RFG

 Arizona CBG

 All Other

Jet Fuel

Diesel Fuel

 CARB Diesel

 EPA Diesel

 Ultra Low Sulfur Diesel

 Other diesel

Unf. Oil to PetroChem 

Carbon Black Feed

Residual Oil

Asphalt

Lubes & Waxes

Coke

Sulfur (s tons/d)

Excessed Material

C5s

Coker Naphtha

FCC Naphtha

Crude Oil Input per

Barrel of Gasoline

Refinery Modeling Results -- Refinery Inputs and Outputs

PADD 1

(K b/d)

2015

2007 Single Octane

Calibration Reference NCG 94 RON 95 RON

Sum Win Sum Win Sum Win Sum Win Sum Win

1,498 1,478 1,455 1,427 1,465 1,432 1,477 1,438 1,487 1,443

263 255 270 281 270 281 273 281 280 281

8 13 8 13 8 13 11 13 18 13

31 31 31 31 31

22

33 21 34 21 34 21 34 21 34 21

56 72 58 74 58 74 58 74 58 74

98 73 100 74 100 74 100 74 100 74

46 45 70 68 70 68 70 68 70 68

26 29 26 29 26 29 26 29

10 10 10 9 10 10 11 10 11 10

33 30 37 34 40 39 39 37 40 37

1,750 1,730 1,730 1,727 1,737 1,729 1,741 1,731 1,745 1,732

20.0 18.0 19.0 17.0 19.0 17.0 19.0 17.0 19.0 17.0

34 32 31 29 32 31 34 33 36 34

19 20 20 20 20 20 20 20 20 20

10 1 21 1 28 1 29 1 32 1

837 848 841 854 841 854 841 854 841 854

459 445 697 677 697 677 697 677 697 677

378 403 144 177 144 177 144 177 144 177

97 104 93 100 93 100 93 100 93 100

494 498 493 497 493 497 493 497 493 497

39 27

273 264 310 289 310 289 310 289 310 289

182 207 183 208 183 208 183 208 183 208

124 116 124 117 124 117 124 117 124 117

97 76 69 74 69 74 69 74 69 74

18 17 18 18 18 18 18 18 18 18

20 21 26 21 27 22 27 22 28 22

1.2 1.2 1.3 1.2 1.3 1.2 1.4 1.2 1.4 1.2

6 14

6 14

1.789 1.743 1.730 1.671 1.742 1.677 1.757 1.684 1.768 1.690

October 8, 2010 Page 1 of 4 MathPro
Single Octane NCG

Exhibit C-3:

Inputs/

Outputs

Crude Oil

Other Inputs

Isobutane

Butane

Butylene

Natural Gas Liquids

Gasoline Blendstocks

Straight Run Naphtha

Kerosene

Heavy Gas Oil

Resid

Ethanol -- RFG

 All Other

Purchased Energy

Electricity (MM Kwh/d)

Natural Gas (K foeb/d)

Refined Products1

Aromatics

Ethane/Ethylene

Propane

Propylene

Butanes/Butylenes

Aviation Gas

Naphtha to PetroChem

Special Naphthas

Gasoline:

 CARBOB

 Federal RFG

 Arizona CBG

 All Other

Jet Fuel

Diesel Fuel

 CARB Diesel

 EPA Diesel

 Ultra Low Sulfur Diesel

 Other diesel

Unf. Oil to PetroChem 

Carbon Black Feed

Residual Oil

Asphalt

Lubes & Waxes

Coke

Sulfur (s tons/d)

Excessed Material

C5s

Coker Naphtha

FCC Naphtha

Crude Oil Input per

Barrel of Gasoline

Refinery Modeling Results -- Refinery Inputs and Outputs

PADD 2

(K b/d)

2015

2007 Single Octane

Calibration Reference NCG 94 RON 95 RON

Sum Win Sum Win Sum Win Sum Win Sum Win

3,249 3,111 3,193 3,058 3,240 3,059 3,294 3,082 3,336 3,105

230 254 243 287 245 287 241 287 237 287

45 43 52 56 53 56 49 56 46 56

67 71 71 71 71

10 10 10 10

55 36 62 40 62 40 62 40 62 40

22 22 20 21 20 21 20 21 20 21

32 15 30 14 30 14 30 14 30 14

46 40 43 37 43 37 43 37 43 37

30 31 37 38 37 38 37 38 37 38

30 36 178 177 178 177 178 177 178 177

25 23 25 23 26 24 26 24 27 25

107 110 120 121 128 126 126 121 124 116

3,431 3,341 3,524 3,458 3,561 3,459 3,559 3,463 3,566 3,470

31.0 29.0 31.0 29.0 31.0 29.0 31.0 29.0 31.0 29.0

82 74 73 65 73 66 78 70 87 77

24 18 25 19 25 19 25 19 25 19

65 71 107 100 98

3333333333

4354545454

1,819 1,825 1,964 1,971 1,964 1,971 1,964 1,971 1,964 1,971

303 314 366 380 366 380 366 380 366 380

1,516 1,511 1,598 1,591 1,598 1,591 1,598 1,591 1,598 1,591

198 203 190 194 190 194 190 194 190 194

922 932 924 932 924 932 924 932 924 932

88 69

792 817 909 916 909 916 909 916 909 916

42 46 15 16 15 16 15 16 15 16

9898989898

76 78 51 54 51 54 51 54 51 54

182 153 161 163 161 163 161 163 161 163

16 15 18 16 18 16 18 16 18 16

99 101 109 102 112 102 115 103 117 104

3.6 3.6 3.7 3.5 3.7 3.5 3.8 3.5 3.9 3.6

27 37

27 37

1.786 1.704 1.626 1.551 1.650 1.552 1.677 1.564 1.698 1.576

October 8, 2010 Page 2 of 4 MathPro
Single Octane NCG

Exhibit C-3:

Inputs/

Outputs

Crude Oil

Other Inputs

Isobutane

Butane

Butylene

Natural Gas Liquids

Gasoline Blendstocks

Straight Run Naphtha

Kerosene

Heavy Gas Oil

Resid

Ethanol -- RFG

 All Other

Purchased Energy

Electricity (MM Kwh/d)

Natural Gas (K foeb/d)

Refined Products1

Aromatics

Ethane/Ethylene

Propane

Propylene

Butanes/Butylenes

Aviation Gas

Naphtha to PetroChem

Special Naphthas

Gasoline:

 CARBOB

 Federal RFG

 Arizona CBG

 All Other

Jet Fuel

Diesel Fuel

 CARB Diesel

 EPA Diesel

 Ultra Low Sulfur Diesel

 Other diesel

Unf. Oil to PetroChem 

Carbon Black Feed

Residual Oil

Asphalt

Lubes & Waxes

Coke

Sulfur (s tons/d)

Excessed Material

C5s

Coker Naphtha

FCC Naphtha

Crude Oil Input per

Barrel of Gasoline

Refinery Modeling Results -- Refinery Inputs and Outputs

PADD 3

(K b/d)

2015

2007 Single Octane

Calibration Reference NCG 94 RON 95 RON

Sum Win Sum Win Sum Win Sum Win Sum Win

7,461 7,004 7,269 6,891 7,371 6,887 7,464 6,974 7,526 7,005

741 1,100 709 1,059 717 1,072 719 1,034 792 1,063

8 138 120 8 133 10 95 83 124

216 216 216 216 216

10 10 10 10 10

98 97 100 100 100 100 100 100 100 100

65 65 65 65 65 65 65 65 65 65

36 28 33 26 33 26 33 26 33 26

12 11 11 11 11

393 385 366 358 366 358 366 358 366 358

65 71 61 66 61 66 61 66 61 66

76 78 84 87 84 87 84 87 84 87

4 7 345 350 345 350 345 350 345 350

61 58 62 59 63 60 63 61 66 63

244 234 269 260 278 270 260 253 275 250

8,007 7,934 8,200 8,191 8,270 8,190 8,285 8,201 8,287 8,218

208.2 178.0 208.0 178.0 208.0 178.0 208.0 178.0 208.0 183.0

19 19 20 20 20 20 20 20 20 20

168 144 154 140 156 139 169 150 181 162

176 188 180 192 180 192 180 192 180 192

38 45 112 115 105

12 11 12 10 12 10 12 10 12 10

34 43 24 31 24 31 24 31 24 31

3,766 3,840 4,211 4,295 4,211 4,295 4,211 4,295 4,211 4,295

757 783 840 870 840 870 840 870 840 870

3,009 3,057 3,371 3,425 3,371 3,425 3,371 3,425 3,371 3,425

787 756 766 738 766 738 766 738 766 738

2,005 2,033 2,058 2,086 2,058 2,086 2,058 2,086 2,058 2,086

496 442

1,211 1,366 1,993 2,037 1,993 2,037 1,993 2,037 1,993 2,037

298 225 65 49 65 49 65 49 65 49

184 185 117 118 117 118 117 118 117 118

25 25 25 25 25 25 25 25 25 25

327 296 216 200 216 200 216 200 216 200

114 80 71 69 71 69 71 69 71 69

144 136 93 89 93 89 93 89 93 89

356 350 382 368 387 368 393 374 399 376

12.4 12.0 12.9 12.4 13.1 12.4 13.3 12.5 13.4 12.6

25 114

25 114

1.981 1.824 1.726 1.604 1.750 1.603 1.772 1.624 1.787 1.631

October 8, 2010 Page 3 of 4 MathPro
Single Octane NCG

Exhibit C-3:

Inputs/

Outputs

Crude Oil

Other Inputs

Isobutane

Butane

Butylene

Natural Gas Liquids

Gasoline Blendstocks

Straight Run Naphtha

Kerosene

Heavy Gas Oil

Resid

Ethanol -- RFG

 All Other

Purchased Energy

Electricity (MM Kwh/d)

Natural Gas (K foeb/d)

Refined Products1

Aromatics

Ethane/Ethylene

Propane

Propylene

Butanes/Butylenes

Aviation Gas

Naphtha to PetroChem

Special Naphthas

Gasoline:

 CARBOB

 Federal RFG

 Arizona CBG

 All Other

Jet Fuel

Diesel Fuel

 CARB Diesel

 EPA Diesel

 Ultra Low Sulfur Diesel

 Other diesel

Unf. Oil to PetroChem 

Carbon Black Feed

Residual Oil

Asphalt

Lubes & Waxes

Coke

Sulfur (s tons/d)

Excessed Material

C5s

Coker Naphtha

FCC Naphtha

Crude Oil Input per

Barrel of Gasoline

Refinery Modeling Results -- Refinery Inputs and Outputs

California

(K b/d)

2015

2007 Single Octane

Calibration Reference NCG 94 RON 95 RON

Sum Win Sum Win Sum Win Sum Win Sum Win

1,683 1,771 1,555 1,581 1,553 1,582 1,594 1,597 1,648 1,617

184 166 200 176 204 176 202 186 206 186

3 4 8 6 10 10 10

20 20 20 20 20

20 23 20 23 20 23 20 23 20 23

51 37 15 10 15 10 15 10 15 10

11111

107 82 153 116 153 116 153 116 153 116

6 86868686

4 1 10 7 10 7 10 7 10 7

19 18 18 17 18 17 19 18 20 19

94 97 99 94 100 94 93 91 98 91

1,829 1,909 1,735 1,743 1,736 1,743 1,752 1,748 1,761 1,752

37 35 33 31 33 31 39 36 42 40

3 1 2 12 18

16 33 12 21 12 21 12 21 12 21

1,051 1,034 967 946 967 946 967 946 967 946

869 960 905 917 905 917 905 917 905 917

28

154 74 62 29 62 29 62 29 62 29

240 282 241 248 241 248 241 248 241 248

356 365 350 358 350 358 350 358 350 358

219 233 249 250 249 250 249 250 249 250

14 4

118 125 101 108 101 108 101 108 101 108

5 3

66 118 63 76 63 76 63 76 63 76

42 25 47 44 47 44 47 44 47 44

18 17 21 19 21 19 21 19 21 19

100 99 94 93 94 93 95 93 99 95

2.9 2.8 2.7 2.7 2.7 2.7 2.8 2.7 2.9 2.8

41

10

30

1.601 1.713 1.608 1.672 1.606 1.672 1.648 1.688 1.705 1.710

October 8, 2010 Page 4 of 4 MathPro
Single Octane NCG

Exhibit C-4:

Property

Octane &

Volume

Property

RVP (psi)Oxygen (wt%)Aromatics (vol%)Benzene (vol%)Olefins (vol%)Sulfur (ppm)E130 (vol% off)E200 (vol% off)E215 (vol% off)E300 (vol% off)E310 (vol% off)Estimated DI1Energy Density2OctaneRONMONCONSensitivityVolume (K b/d)

Refinery Modeling Results -- Pool Gasoline PropertiesPADD 1

2015

2007 Sin

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Winter 

RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG P

6.8 8.2 7.4 12.0 12.0 12.0 6.8 8.6 7.1 12.0 12.0 12.0 6.8 7.1 6.9 12.0 12.0 12.0 6.7 7.1 6.8 12.0 12.0 3.3 0.0 1.8 3.3 0.0 1.7 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 

19.2 28.5 23.4 19.3 22.9 21.0 18.9 26.5 20.2 16.3 22.6 17.6 19.8 28.5 21.3 16.0 19.8 16.8 22.2 28.5 23.3 16.1 28.5 0.51 0.91 0.69 0.51 0.91 0.70 0.51 0.62 0.53 0.51 0.62 0.53 0.51 0.62 0.53 0.51 0.62 0.53 0.51 0.62 0.53 0.51 0.62 016.9 7.9 12.9 16.6 13.2 15.0 12.7 13.2 12.8 14.8 13.2 14.4 11.6 4.0 10.3 13.3 4.0 11.4 13.2 4.0 11.6 13.0 4.9 

25 17 22 25 25 25 25 25 25 25 23 25 5 5 5 5 5 5 5 5 5 5 5 

8.1 9.1 8.5 16.1 17.0 16.5 8.0 10.8 8.5 17.0 15.5 16.7 8.3 6.4 8.0 17.1 12.1 16.1 8.0 7.2 7.9 17.1 12.5 

45.6 43.7 44.7 55.8 46.5 51.4 46.3 50.0 46.9 55.8 57.7 56.2 46.7 46.2 46.6 52.9 60.3 54.5 45.5 48.0 45.9 52.8 59.5 577.9 80.4 79.0 82.2 80.4 81.3 79.5 81.5 79.9 82.4 83.8 82.7 79.4 80.4 79.5 83.7 91.0 85.2 79.7 80.4 79.8 85.6 83.9 8

1,202 1,177 1191 1,083 1,127 1104 1,191 1,147 1183 1,078 1,066 1076 1,188 1,195 1189 1,093 1,036 1081 1,196 1,179 1193 1,087 1,066 1

5.074 5.217 5.138 4.995 5.134 5.061 5.075 5.084 5.077 4.979 5.002 4.983 5.080 5.117 5.086 4.979 4.967 4.977 5.093 5.106 5.095 4.973 5.021 4.

93.7 91.8 92.9 93.4 92.1 92.7 93.0 93.0 93.0 92.8 92.7 92.8 93.2 92.4 93.0 93.1 91.3 92.7 94.0 94.0 94.0 94.0 94.0 983.1 84.4 83.7 83.4 84.1 83.8 83.6 83.0 83.5 83.8 83.3 83.7 83.4 83.6 83.5 83.5 84.7 83.7 83.9 85.6 84.2 84.4 85.9 888.4 88.1 88.3 88.4 88.1 88.3 88.3 88.0 88.2 88.3 88.0 88.2 88.3 88.0 88.2 88.3 88.0 88.2 89.0 89.8 89.1 89.2 90.0 810.6 7.4 9.2 9.9 7.9 9.0 9.4 9.9 9.5 9.0 9.5 9.1 9.7 8.7 9.6 9.6 6.6 9.0 10.1 8.4 9.8 9.6 8.1 

459 378 837 445 403 848 697 144 841 677 177 854 697 144 841 677 177 854 697 144 841 677 177 

1 ASTM Driveability Index: calculated by formula using modeling results for E130, E215, & E310 for CARBOB and E130, E200, & E300 plus an ethanol adjustment (2.403 for each percent of ethanol in the finished blend) for all other gasoline.2 Million Btu per barrel.

October 8, 2010 Page 1 of 4 
Single Octane NCG

Exhibit C-4:

Property

Octane &

Volume

Property

RVP (psi)Oxygen (wt%)Aromatics (vol%)Benzene (vol%)Olefins (vol%)Sulfur (ppm)E130 (vol% off)E200 (vol% off)E215 (vol% off)E300 (vol% off)E310 (vol% off)Estimated DI1Energy Density2OctaneRONMONCONSensitivityVolume (K b/d)

Refinery Modeling Results -- Pool Gasoline PropertiesPADD 2

2015

2007 Sin

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Winter 

RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG P

6.9 8.7 8.4 13.8 13.7 13.7 6.9 8.7 8.4 13.8 13.7 13.7 6.9 7.5 7.4 13.8 13.7 13.7 6.9 7.5 7.4 13.8 13.7 3.3 0.7 1.1 3.3 0.8 1.2 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 

16.0 29.3 27.0 16.0 24.8 23.3 21.6 20.4 20.6 16.0 17.1 16.9 16.0 23.4 22.0 16.0 17.3 17.1 16.0 26.9 24.9 18.8 20.4 20.84 1.37 1.28 0.79 0.92 0.90 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 0.62 011.4 8.1 8.7 11.1 9.3 9.6 3.4 8.7 7.7 10.9 7.6 8.2 12.1 4.6 6.0 12.0 5.7 6.9 5.5 6.5 6.3 5.7 6.8 

25 17 18 25 15 17 9 19 17 25 14 16 5 5 5 5 5 5 5 5 5 5 5 

9.6 9.3 9.4 20.0 18.3 18.6 6.6 10.4 9.7 19.2 18.5 18.7 8.5 8.1 8.2 17.9 18.7 18.6 7.2 8.5 8.3 20.5 17.9 

54.0 47.5 48.5 61.3 56.9 57.7 54.0 50.1 50.8 55.4 59.8 58.9 49.2 49.8 49.7 56.7 59.5 59.0 47.3 50.0 49.5 61.3 58.6 582.0 81.2 81.3 82.4 83.8 83.5 84.9 82.0 82.5 82.0 85.7 85.0 83.7 80.9 81.5 81.4 85.9 85.0 82.2 80.8 81.1 82.0 85.6 8

1,122 1,152 1147 1,028 1,042 1040 1,124 1,146 1142 1,074 1,033 1041 1,153 1,161 1159 1,072 1,033 1041 1,177 1,159 1162 1,028 1,044 1

5.048 5.163 5.144 4.930 5.057 5.035 5.037 5.031 5.032 4.945 4.930 4.933 5.041 5.063 5.059 4.933 4.931 4.931 5.014 5.089 5.075 4.962 4.944 4.

92.7 92.9 92.9 92.9 92.7 92.7 91.7 92.4 92.2 92.7 91.9 92.1 93.1 92.1 92.3 93.2 91.8 92.1 94.0 94.0 94.0 94.0 94.0 984.1 84.9 84.8 83.9 85.1 84.9 84.9 83.6 83.9 83.9 84.1 84.0 83.5 83.9 83.8 83.4 84.2 84.0 86.0 84.6 84.9 86.0 85.5 888.4 88.9 88.8 88.4 88.9 88.8 88.3 88.0 88.1 88.3 88.0 88.1 88.3 88.0 88.1 88.3 88.0 88.1 90.0 89.3 89.4 90.0 89.7 8

8.6 8.0 8.1 9.0 7.6 7.8 6.8 8.7 8.4 8.9 7.9 8.1 9.5 8.2 8.5 9.7 7.6 8.0 8.0 9.4 9.1 8.0 8.5 

303 1516 1819 314 1511 1825 366 1598 1964 380 1591 1971 366 1598 1964 380 1591 1971 366 1598 1964 380 1591 1

1 ASTM Driveability Index: calculated by formula using modeling results for E130, E215, & E310 for CARBOB and E130, E200, & E300 plus an ethanol adjustment (2.403 for each percent of ethanol in the finished blend) for all other gasoline.2 Million Btu per barrel.

October 8, 2010 Page 2 of 4 
Single Octane NCG

Exhibit C-4:

Property

Octane &

Volume

Property

RVP (psi)Oxygen (wt%)Aromatics (vol%)Benzene (vol%)Olefins (vol%)Sulfur (ppm)E130 (vol% off)E200 (vol% off)E215 (vol% off)E300 (vol% off)E310 (vol% off)Estimated DI1Energy Density2OctaneRONMONCONSensitivityVolume (K b/d)

Refinery Modeling Results -- Pool Gasoline PropertiesPADD 3

2015

2007 Sin

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Winter 

RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG P

6.9 8.3 8.0 11.8 11.9 11.9 6.9 8.7 8.4 11.8 11.9 11.9 6.8 7.4 7.3 11.8 11.9 11.9 6.8 7.4 7.3 11.8 11.9 3.3 0.0 0.7 3.3 0.1 0.7 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 3.3 

16.0 27.0 24.8 16.0 21.5 20.4 16.0 19.3 18.6 16.0 16.3 16.2 16.5 21.5 20.5 17.9 15.3 15.9 16.0 24.5 22.8 21.2 17.6 0.55 0.97 0.89 0.53 0.87 0.80 0.55 0.55 0.55 0.54 0.55 0.55 0.43 0.62 0.58 0.54 0.54 0.54 0.52 0.62 0.60 0.54 0.52 010.7 11.3 11.2 10.0 10.3 10.3 11.7 9.7 10.1 12.5 7.6 8.6 9.0 7.4 7.8 4.5 7.9 7.2 8.4 7.5 7.7 7.0 8.0 

25 23 23 23 22 22 25 21 21 25 17 19 5 5 5 5 5 5 5 5 5 5 5 

7.4 9.0 8.6 15.8 15.9 15.9 7.5 10.5 9.9 17.3 16.8 16.9 7.5 8.7 8.5 16.2 17.1 16.9 7.9 8.1 8.1 16.9 16.0 

50.6 42.4 44.1 57.2 49.3 50.9 54.0 50.1 50.9 58.8 57.3 57.6 54.0 50.1 50.9 65.0 56.0 57.9 48.9 49.5 49.4 58.8 56.3 581.5 79.5 79.9 82.0 83.9 83.5 81.9 83.0 82.8 87.1 85.1 85.5 81.5 81.6 81.6 85.0 85.7 85.6 88.8 78.7 80.7 82.7 85.7 8

1,157 1,190 1184 1,075 1,099 1094 1,131 1,142 1140 1,040 1,059 1055 1,132 1,154 1150 1,008 1,065 1053 1,140 1,171 1165 1,057 1,067 1

5.038 5.207 5.173 4.950 5.113 5.080 5.021 5.030 5.028 4.978 4.952 4.957 5.028 5.067 5.060 4.956 4.955 4.955 5.037 5.072 5.065 4.994 4.949 4.

92.7 92.0 92.2 92.7 91.6 91.8 92.4 92.4 92.4 92.3 91.9 92.0 92.4 92.5 92.5 91.7 92.1 92.0 94.0 94.0 94.0 94.0 94.0 983.7 83.8 83.7 83.7 84.2 84.1 83.8 83.6 83.6 83.9 84.1 84.0 83.8 83.5 83.6 84.5 83.9 84.0 85.8 84.5 84.8 85.2 85.6 888.2 87.9 88.0 88.2 87.9 88.0 88.1 88.0 88.0 88.1 88.0 88.0 88.1 88.0 88.0 88.1 88.0 88.0 89.9 89.2 89.4 89.6 89.8 8

9.1 8.3 8.4 9.0 7.3 7.7 8.6 8.8 8.8 8.5 7.8 8.0 8.6 9.0 8.9 7.1 8.2 8.0 8.2 9.5 9.2 8.8 8.4 

757 3009 3766 783 3057 3840 840 3371 4211 870 3425 4295 840 3371 4211 870 3425 4295 840 3371 4211 870 3425 4

1 ASTM Driveability Index: calculated by formula using modeling results for E130, E215, & E310 for CARBOB and E130, E200, & E300 plus an ethanol adjustment (2.403 for each percent of ethanol in the finished blend) for all other gasoline.2 Million Btu per barrel.

October 8, 2010 Page 3 of 4 
Single Octane NCG

Exhibit C-4:

Property

Octane &

Volume

Property

RVP (psi)Oxygen (wt%)Aromatics (vol%)Benzene (vol%)Olefins (vol%)Sulfur (ppm)E130 (vol% off)E200 (vol% off)E215 (vol% off)E300 (vol% off)E310 (vol% off)Estimated DI1Energy Density2OctaneRONMONCONSensitivityVolume (K b/d)

Refinery Modeling Results -- Pool Gasoline PropertiesCalifornia

2015

2007 

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Winte

Carbob CBG CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG 

5.6 6.8 8.0 6.0 10.0 11.0 10.1 5.6 8.3 5.8 10.0 11.0 10.0 5.6 6.9 5.7 10.0 11.0 10.0 5.5 6.9 5.6 10.0 11.0 0.0 0.0 0.9 0.1 0.0 0.4 0.0 0.0 3.3 0.2 0.0 3.3 0.1 0.0 3.3 0.2 0.0 3.3 0.1 0.0 3.3 0.2 0.0 3.3 

23.5 25.2 30.8 24.6 22.8 30.3 23.3 21.1 22.8 21.2 20.0 26.4 20.2 21.2 25.8 21.5 20.5 23.7 20.6 27.6 30.8 27.8 24.0 30.8 0.58 0.65 0.61 0.59 0.58 0.61 0.58 0.58 0.62 0.58 0.58 0.62 0.58 0.58 0.62 0.58 0.58 0.62 0.58 0.58 0.62 0.58 0.58 0.62 

5.7 9.6 6.8 6.0 6.8 6.8 6.8 5.7 6.8 5.8 8.5 6.8 8.4 4.8 1.7 4.6 7.5 6.8 7.4 4.9 6.8 5.1 7.0 1.5 

10 19 18 11 10 17 11 7 14 8 7 18 7 5 5 5 5 5 5 5 5 5 5 5 

7.5 11.0 8.7 7.8 13.2 9.5 12.9 6.7 13.6 7.1 14.4 14.0 14.3 6.6 10.4 6.9 14.6 13.7 14.6 6.9 7.9 7.0 13.2 14.3 

40.5 41.2 42.5 40.8 45.0 44.7 45.0 38.5 52.9 39.4 46.4 52.6 46.6 38.7 42.5 38.9 46.3 54.3 46.6 39.0 43.0 39.2 45.2 48.0 49.9 53.8 48.3 49.7 52.7 51.0 52.6 48.0 58.1 48.7 54.0 55.2 54.0 48.0 50.9 48.2 53.9 58.3 54.0 48.3 48.9 48.3 53.4 52.8 86.5 85.5 79.8 85.5 86.0 79.8 85.6 84.9 79.8 84.5 86.3 79.8 86.1 84.7 79.8 84.4 86.0 79.8 85.8 84.3 79.8 84.0 87.7 79.8 89.6 88.2 83.3 88.7 89.1 80.5 88.5 88.1 80.5 87.6 89.0 83.5 88.8 88.0 81.0 87.5 88.8 80.9 88.6 87.5 82.5 87.2 90.8 80.5 

1,182 1,168 1,196 1183 1,125 1,174 1128 1,206 1,122 1201 1,113 1,123 1113 1,208 1,207 1208 1,114 1,112 1113 1,204 1,213 1205 1,116 1,153 

5.228 5.175 5.241 5.229 5.169 5.245 5.175 5.228 5.038 5.216 5.154 5.075 5.151 5.230 5.052 5.219 5.154 5.036 5.150 5.258 5.136 5.250 5.174 5.071 

89.0 91.9 92.2 89.6 89.1 92.5 89.3 87.4 92.1 87.7 87.6 91.9 87.7 87.4 91.9 87.6 87.6 91.9 87.7 90.7 94.0 90.9 90.7 94.0 82.8 84.3 84.8 83.1 82.7 84.5 82.9 81.6 83.7 81.7 81.4 83.9 81.5 81.6 83.9 81.8 81.4 83.9 81.5 84.0 86.0 84.1 84.0 85.6 85.9 88.1 88.5 86.3 85.9 88.5 86.1 84.5 87.9 84.7 84.5 87.9 84.6 84.5 87.9 84.7 84.5 87.9 84.6 87.3 90.0 87.5 87.3 89.8 

6.3 7.7 7.3 6.5 6.3 8.0 6.4 5.8 8.3 6.0 6.2 8.0 6.2 5.7 8.0 5.9 6.1 8.0 6.2 6.7 8.0 6.8 6.7 8.4 

869 28 154 1051 960 74 1034 905 62 967 917 29 946 905 62 967 917 29 946 905 62 967 917 29 

Note: An octane senstivity for Carbob of about 6.8 would increase to about 8.0 when blended with 10% ethanol.1 ASTM Driveability Index: calculated by formula using modeling results for E130, E215, & E310 for CARBOB and E130, E200, & E300 plus an ethanol adjustment (2.403 for each percent of ethanol in the finished blend) for all other gasoline.2 Million Btu per barrel.

October 8, 2010 Page 4 of 4 
Single Octane NCG

Exhibit C-5: Refinery Modeling Results -- Average Aromatics Content of the Gasoline Pool,

PADDs 1-3, California, and Combined Regions

PADDs 1-3 California 

2007 2015 2007 2015 2007 

Calibra- Refer- 94 95 Calibra- Refer- 94 95 Calibra- Refer- 

tion ence NCG RON RON tion ence NCG RON RON tion ence 

Summer 25.2 19.4 21.0 23.5 25.4 24.6 21.2 21.5 27.8 29.0 25.1 19.6 Winter 21.3 16.6 16.3 18.8 20.6 23.3 20.2 20.6 24.2 24.2 21.6 17.0 Annual 23.2 18.0 18.6 21.1 23.0 24.2 20.9 21.2 26.6 27.5 23.4 18.3 

Note: California average reflects CARBOB, not finished RFG.

October 8, 2010 
Single Octane NCG

Exhibit C-6:

Gasoline

Blendstock

Total (%)C4sNatural Gas LiquidsIsomerateRaffinateNaphthas (C5-250°)HydrocrackateAlkylatePoly GasFCC NaphthaReformatePy GasEthanol

Volume (K b/d)

Refinery Modeling Results -- Gasoline Composition (Vol. %)PADD 1

2015

2007 S

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Winter 

RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG 

100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 

0.9 5.9 3.2 10.1 14.7 12.3 1.0 4.2 1.5 11.4 9.5 11.0 0.9 1.5 1.0 10.9 6.7 10.0 0.8 2.2 1.0 10.8 7.4 2.8 1.2 2.1 3.8 2.0 2.4 2.0 2.5 2.0 2.4 2.0 2.5 2.0 2.4 2.0 2.5 0.4 0.9 0.6 0.3 2.1 1.2 0.3 0.2 0.2 2.0 0.6 1.2 0.2 0.3 2.6 0.7 1.4 0.2 0.3 2.8 4.7 18.4 11.1 11.4 8.5 10.0 10.7 14.5 11.4 9.0 17.8 10.9 9.9 20.9 11.8 5.5 31.9 11.0 8.2 25.5 11.2 3.9 32.9 1.7 0.9 2.5 1.2 1.2 1.0 2.1 1.6 1.1 0.9 1.6 1.3 0.9 0.7 1.6 8.4 16.0 11.9 5.4 12.7 8.9 13.9 11.5 10.9 8.7 12.7 5.9 11.5 8.6 13.0 9.5 11.6 13.2 11.8 11.0 6.7 4.1 2.2 1.5 2.0 1.8 2.3 0.9 2.0 2.2 1.8 1.2 2.5 1.5 1.8 1.5 1.8 1.4 2.6 1.6 2.1 0.6 

56.0 26.5 42.3 42.0 39.2 40.7 40.9 44.3 41.5 38.7 39.6 38.9 47.0 7.5 40.3 45.8 36.3 47.4 6.9 40.5 46.3 10.4 31.1 20.0 15.4 18.2 16.7 17.3 22.7 18.3 13.0 21.1 14.7 14.8 47.5 20.4 13.0 34.3 17.4 17.4 32.0 19.9 11.5 39.0 10.5 5.6 10.0 5.2 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 

437 378 815 445 403 848 697 144 841 677 177 854 697 144 841 677 177 854 697 144 841 677 177 

October 8, 2010 Page 1 of 4 
Single Octane NCG

Exhibit C-6:

Gasoline

Blendstock

Total (%)C4sNatural Gas LiquidsIsomerateRaffinateNaphthas (C5-250°)HydrocrackateAlkylatePoly GasFCC NaphthaReformatePy GasEthanol

Volume (K b/d)

Refinery Modeling Results -- Gasoline Composition (Vol. %)PADD 2

2015

2007 S

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Winter 

RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG 

100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 

0.9 5.7 4.9 15.7 15.5 15.5 0.9 4.1 3.5 13.1 14.1 13.9 0.5 2.0 1.7 12.3 14.0 13.7 0.5 2.1 1.8 15.3 13.2 

3.0 0.6

0.1 11.2 9.4 3.9 10.5 9.3 10.9 8.2 8.7 6.3 7.6 7.4 6.9 9.1 8.7 6.5 7.2 7.1 10.1 8.4 8.7 9.2 

0.7 0.6 0.5 0.5 0.5 0.8 0.8 0.8 1.1 0.9 0.2 0.2 1.1 0.9 0.2 0.2 0.3 0.8 7.5 6.2 10.9 6.9 7.6 14.3 4.8 6.6 8.6 6.9 7.3 8.8 8.5 4.5 7.6 7.0 10.3 6.6 7.3 8.5 6.6 

14.6 2.7 4.7 5.6 4.6 10.3 6.1 6.9 6.5 6.6 6.6 6.0 4.9 8.1 6.6 3.8 3.1 7.5 3.5 22.3 11.3 13.1 5.6 10.1 9.3 21.3 10.1 12.2 5.6 10.9 9.9 14.4 11.8 12.3 4.3 11.4 10.0 28.0 8.6 12.2 19.9 7.9 

0.7 0.2 0.3 0.2 0.2 0.5 0.2 0.3 0.5 0.2 0.3 0.3 0.3 0.2 

41.6 26.4 29.0 43.3 19.8 23.9 4.4 31.3 26.3 43.4 16.3 21.5 53.5 19.3 25.7 51.8 14.3 21.5 26.0 26.7 26.6 12.9 24.0 

9.9 32.2 28.5 10.1 28.6 25.4 26.5 24.1 24.6 15.1 24.8 22.9 6.9 31.2 26.7 7.6 26.2 22.6 15.1 31.9 28.7 25.6 24.6 

10.0 2.0 3.3 10.0 2.4 3.7 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 

303 1516 1819 314 1511 1825 366 1598 1964 380 1591 1971 366 1598 1964 380 1591 1971 366 1598 1964 380 1591 

October 8, 2010 Page 2 of 4 
Single Octane NCG

Exhibit C-6:

Gasoline

Blendstock

Total (%)C4sNatural Gas LiquidsIsomerateRaffinateNaphthas (C5-250°)HydrocrackateAlkylatePoly GasFCC NaphthaReformatePy GasEthanol

Volume (K b/d)

Refinery Modeling Results -- Gasoline Composition (Vol. %)PADD 3

2015

2007 S

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Winter 

RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG Pool RFG CG 

100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 

0.5 4.5 3.7 10.2 12.7 12.2 0.5 3.4 2.8 9.2 11.2 10.8 0.5 1.3 1.2 10.9 10.8 10.8 0.5 1.6 1.3 8.4 10.8 

0.1 0.1

8.8 5.5 6.1 11.8 4.5 6.0 15.3 3.1 5.5 6.8 5.4 20.6 1.7 5.5 12.9 3.5 5.4 6.2 10.6 9.7 6.1 10.0 2.9 2.8 2.8 1.9 2.3 2.2 2.8 2.2 0.4 0.3 0.6 0.4 0.4 0.3 0.9 0.7 1.6 2.2 9.1 7.7 5.9 7.6 7.2 4.5 10.7 9.5 6.1 13.5 12.0 16.1 12.9 16.3 10.8 11.9 12.5 5.9 7.2 6.3 6.6 

1.7 1.4 3.0 2.4 6.4 5.1 9.2 4.4 5.3 3.5 2.8 1.4 5.5 4.6 3.0 2.4 12.6 

20.0 14.0 15.2 7.7 16.8 14.9 16.6 12.9 13.6 11.4 13.3 12.9 18.7 12.5 13.7 12.8 13.4 13.3 25.3 10.9 13.8 10.9 14.0 

0.6 0.5 0.1 0.1 0.5 0.4 0.2 0.2 0.2 

43.5 35.5 37.1 39.5 33.3 34.6 44.5 31.1 33.8 36.6 26.6 28.6 40.7 32.2 33.9 8.0 34.6 29.2 32.7 33.6 33.4 21.3 33.7 12.1 24.6 22.1 13.0 18.0 17.0 8.7 17.8 16.0 17.5 12.5 13.5 9.5 20.8 18.5 27.8 9.7 13.4 12.8 22.0 20.1 19.2 13.0 

1.5 1.2 1.5 1.2 1.3 1.1 1.3 1.0 1.3 1.1 1.3 1.0 1.3 1.1 5.2 

10.0 0.1 2.1 10.0 0.2 2.2 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 10.0 

757 3009 3766 783 3057 3840 840 3371 4211 870 3425 4295 840 3371 4211 870 3425 4295 840 3371 4211 870 3425 

October 8, 2010 Page 3 of 4 
Single Octane NCG

Exhibit C-6:

Gasoline

Blendstock

Total (%)C4sNatural Gas LiquidsIsomerateRaffinateNaphthas (C5-250°)HydrocrackateAlkylatePoly GasFCC NaphthaReformatePy GasEthanol

Volume (K b/d)

Refinery Modeling Results -- Gasoline Composition (Vol. %)California

2015

2007 

Calibration Reference NCG 94 RON 

Summer Winter Summer Winter Summer Winter Summer Wint

Carbob CBG CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG Pool Carbob CG 

100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 100 10

0.5 4.5 3.3 0.8 8.7 7.6 8.7 0.9 3.8 1.1 9.6 10.1 9.6 0.8 4.0 1.0 9.8 9.2 9.8 0.5 0.5 0.5 8.0 6

12.6 14.8 10.8 12.6 10.9 10.1 9.0 18.1 9.6 10.1 9.7 8.8 12.6 9.0 10.7 10.4 10.0 9.4 9.8 

1.7 3.7 2.7 1.8 1.9 10.7 2.5 1.5 12.3 2.2 2.1 18.4 2.6 2.2 13.1 2.9 1.8 31.8 2.7 1.1 18.5 2.2 1.8 

10.2 9.5 9.0 8.4 13.2 12.3 13.0 12.6 12.2 11.4 12.6 12.2 9.2 8.7 8.2 2717.7 16.4 12.9 12.0 18.7 17.5 10.4 10.1 19.7 18.4 10.3 10.0 18.2 16.8 18.2 13.7 

0.3 0.3 0.5 0.5 0.5 0.5 0.5 0.5 1.1 0.1 1.0 

29.3 33.6 24.6 29.3 28.2 33.4 28.6 30.3 26.3 30.1 28.1 43.9 28.6 29.6 22.1 29.1 28.3 16.8 28.0 30.6 30.3 30.6 28.6 826.8 30.2 48.9 27.9 26.9 46.2 28.3 25.5 26.8 25.6 25.4 17.5 25.2 26.1 31.8 26.4 25.3 30.3 25.5 29.2 22.8 28.8 28.4 47

1.4 0.1 10.0 0.6 10.0 0.3 10.0 0.6 10.0 0.3 10.0 0.6 10

836 28 38 902 941 74 1015 905 62 967 917 29 946 905 62 967 917 29 946 905 62 967 917 2

October 8, 2010 Page 4 of 4 
Single Octane NCG

Exhibit C-7: Prices for Crude Oil, C4s, and Distressed Blendstocks, by Region

($/bbl, except as noted)

2015

2007 Single Octane

Product/ Calibration Reference NCG 94 RON 95 RON

Blendstock Sum Win Sum Win Sum Win Sum Win Sum Win

PADD 1

Composite Crude 71.63 90.45 105.30 105.30 105.30 105.30 105.30 105.30 105.30 105.30

Iso-butane 59.05 76.53 76.10 80.44 76.10 80.44 76.10 80.44 76.10 80.44

Butane 59.05 76.53 76.10 80.44 76.10 80.44 76.10 80.44 76.10 80.44

Distressed Blendstocks

 C5s 72.09 72.09 72.09

 Coker Naphtha

 FCC Naphtha

Octane (¢/oct gal)

RON 3.32 1.32 6.63 2.27

CON 3.29 1.57 1.75 0.87 1.84 0.67

Value above Price on

Volume Constrained C4s

Iso-butane 7.89 11.75 26.80 25.17 23.11

Butane 9.65 13.88 27.85 25.61 21.89

PADD 2

Composite Crude 65.92 86.69 100.51 100.51 100.51 100.51 100.51 100.51 100.51 100.51

Iso-butane 63.65 79.16 79.14 83.55 79.14 83.55 79.14 83.55 79.14 83.55

Butane 60.04 77.53 77.09 81.44 77.09 81.44 77.09 81.44 77.09 81.44

Distressed Blendstocks

 C5s 73.08 73.08 73.08

 Coker Naphtha

 FCC Naphtha

Octane (¢/oct gal)

RON 2.74 1.46 6.14 2.58

CON 1.85 1.85 1.22 0.76 2.37 0.76

Value above Price on

Volume Constrained C4s

Iso-butane 9.27 9.79 10.27 12.26 10.85

Butane 13.21 14.14 14.40 14.24 14.06

PADD 3

Composite Crude 66.54 87.38 99.49 99.49 99.49 99.49 99.49 99.49 99.49 99.49

Iso-butane 61.65 77.16 77.14 81.55 77.14 81.55 77.14 81.55 77.14 81.55

Butane 58.04 75.53 75.09 79.44 75.09 79.44 75.09 79.44 75.09 79.44

Distressed Blendstocks

 C5s 75.09 75.09 75.09

 Coker Naphtha

 FCC Naphtha

Octane (¢/oct gal)

RON 3.73 2.08 7.46 3.62

CON 2.76 1.62 1.41 0.76 1.90 0.75

Value above Price on

Volume Constrained C4s

Iso-butane

Butane 4.69 2.04 4.25 2.04 8.33 2.04 3.56 2.04 3.28

California

Composite Crude 67.37 87.69 101.22 101.22 101.22 101.22 101.22 101.22 101.22 101.22

Iso-butane 66.97 87.51 83.88 93.45 83.88 93.45 83.88 93.45 83.88 93.45

Butane 45.96 69.92 60.51 73.54 60.51 73.54 60.51 73.54 60.51 73.54

Distressed Blendstocks

 C5s 60.50 60.50 60.50

 Coker Naphtha 59.00 59.00 59.00

 FCC Naphtha 76.00 76.00 76.00

Octane (¢/oct gal)

RON 3.98 3.78 10.24 7.89

CON 1.50 1.77 1.26 1.35 1.68 1.29

Value above Price on

Volume Constrained C4s

Iso-butane 2.73 9.55 24.69

Butane 19.33 20.61 18.93 24.48 39.64

October 8, 2010 MathPro
Single Octane NCG

Exhibit C-8: Backup to Table 1.3 -- Estimated Effects of NCG and Single Octane NCG Standards

PADDs 1-3 California 

Conver- Single Octane Single Octane 

sion Refer- 94 RON 95 RON Refer- 94 RON 95 RON Refer- 

Factors ence NCG NCG NCG ence NCG NCG NCG ence 

Effects on CostsGasoline Volume (K b/d) 7,068 7,068 7,068 7,068 960 960 960 960 8,028 Change in Refining CostTotal ($K/d) 9,274 17,638 27,232 137 2,695 5,818 

 Capital charge & fixed cost 3,390 3,717 5,471 1 139 762  Reduction in Cash Flow1 5,883 13,921 21,761 137 2,556 5,056 

Per gallon of gasoline (¢/gal) 3.1 5.9 9.2 0.3 6.7 14.4 Value of Increase in Gasoline

Energy Density (¢/gal) 0.7 1.1 2.0 0.1 1.5 2.1 

Gasoline Energy Density (MM btu/b) 4.994 5.006 5.014 5.029 5.195 5.196 5.224 5.232 5.018 Cost Savings ($K/d) 1,984 3,326 6,039 32 599 828 

 

Refinery Investment ($B) 4.3 4.7 6.9 0.0 0.2 0.9 

Effects on Refining OperationsCrude Oil InputVolume (K b/d) 11,647 11,727 11,865 11,951 1,564 1,562 1,595 1,638 13,211 

 

Change per Barrel of Gasoline (b/b) 0.01 0.03 0.04 0.00 0.03 0.08 Fuel & Power UseGases -- Natural & Refinery (foeb/d) Natural Gas 273 292 283 295 38 38 36 37 311  Refinery Gases 382 389 415 428 77 77 84 91 459 Catalyst Coke (K b/d) 185 186 192 193 27 26 28 29 212 Power (MM Kwh/d) 95 96 97 101 18 18 18 20 113 On-Purpose HydrogenProduction (MM scf/d) 3,512 3,540 3,275 3,133 1,219 1,218 1,145 1,202 4,731 

October 8, 2010 Page 1 of 2 
Single Octane NCG

Exhibit C-8: Backup to Table 1.3 -- Estimated Effects of NCG and Single Octane NCG Standards

PADDs 1-3 California 

Conver- Single Octane Single Octane 

sion Refer- 94 RON 95 RON Refer- 94 RON 95 RON Refer- 

Factors ence NCG NCG NCG ence NCG NCG NCG ence 

Energy Use (Billion btu/d) 6,193 6,372 6,527 6,719 1,059 1,064 1,111 1,182 7,251 

 

Gases -- Natural & Refinery Natural Gas 6.3 1,720 1,837 1,784 1,857 237 241 229 231 1,957 

 

 Refinery Gases 6.3 2,409 2,454 2,616 2,696 485 485 531 576 2,894 

 

Catalyst Coke 6.02 1,115 1,120 1,154 1,162 160 159 167 177 1,274 

 

Power 9.977 949 961 973 1,005 177 178 184 197 1,126 

 

Percent Increase 3% 5% 9% 0% 5% 12% CO2 Emissions (K MT/d) 487 498 505 514 94 94 96 102 581 Gases -- Natural & Refinery Natural Gas 0.335 91 98 95 99 13 13 12 12 104  Refinery Gases 0.405 155 158 168 173 31 31 34 37 186 Catalyst Coke 0.626 116 116 120 121 17 17 17 18 132 Power 0.638 60.7 61 62 64 11 11 12 13 72 Hydrogen Production 0.018 64 65 60 57 22 22 21 22 87 Percent Increase 2% 4% 6% 0% 3% 9% 

1 Cash Flow is defined here as refinery revenues (from the sale of refined products) less all direct (non-investment related) costs, such as purchases of crude oil, unfinished oils, gasoline blendstocks, natural gas, electricty, and catalysts.Notes: California gasoline energy density reflects mostly CARBOB, rather than finished gasoline blended with 10% ethanol. Energy conversion factors are in terms of MM btu/unit; CO2 conversion factors are in terms of MT/unit. Energy conversion factor for electricity is equal to (3412 btu/Kwh)/((.38 generation efficiency)*(90% transmission efficiency))

October 8, 2010 Page 2 of 2 
Single Octane NCG

Exhibit C-9: Selected 2007 Calibration Results vs. Reported Information

PADD 1 PADD 2 PADD 3 

Summer Winter Summer Winter Summer Winter 

Reported Calibration Reported Calibration Reported Calibration Reported Calibration Reported Calibration Reported Calibration Rep

Crude Inputs (K b/d) 1534 1,498 1511 1,478 3265 3,249 3140 3,111 7383 7,461 7158 7,004 OperationsCharge Rates (K/b/d) Fluid Cat Cracking 653 675 653 665 1062 1,040 960 968 2670 2,625 2662 2,527 

 Hydrocracking 33 29 32 31 258 258 254 254 514 512 509 512  Coking 88 82 88 82 304 301 309 308 1163 1,185 1096 1,185 Operating Indices FCC Conversion 68.2 70.2 75.7 69.8 73.6 72.8  Reformer Severity 100.6 100.1 100.6 100.4 100.5 100.0 Coke Make (K b/d)

Catalyst 33 30 35 31 44 48 41 41 114 119 117 114 Marketable 20 20 23 21 96 99 100 101 353 356 335 350 Prices/Marginal Cost ($/b)Gasoline1RFG 91.99 82.62 98.37 98.78 76.18 99.94 93.05 78.33 99.20 94.66 9Conventional 89.45 80.80 98.99 97.88 75.56 101.96 89.78 77.49 93.05 94.13 Distillates Jet Fuel 90.01 78.16 115.28 97.46 72.20 108.56 88.71 78.37 112.73 99.11 9 CARB Diesel 9 EPA Diesel 88.04 77.96 112.80 97.47 72.34 99.30 87.96 78.47 111.63 100.56 Off-road Diesel 83.82 77.27 109.97 96.51 71.79 97.86 83.11 77.96 108.09 100.06Prem/Reg Differential (¢/g)2RFG 22 16 18 8 16 9 15 9 22 14 21 8 Conventional 23 16 19 8 18 9 17 9 25 14 20 8Pool Gasoline Properties3RVP (psi) 7.4 7.4 12.0 8.3 8.4 13.7 7.9 8.0 11.9 Oxygen (wt%) 1.8 1.8 1.6 1.7 0.7 1.1 0.8 1.2 0.6 0.7 0.5 0.7 Aromatics (vol%) 24.0 23.4 21.4 21.0 27.2 27.0 23.8 23.3 25.4 24.8 22.7 20.4 Benzene (vol%) 0.67 0.69 0.69 0.70 1.30 1.28 1.23 0.90 0.87 0.89 0.80 0.80 Olefins (vol%) 13.5 12.9 14.9 15.0 8.3 8.7 8.0 9.6 12.0 11.2 12.0 10.3 Sulfur (ppm) 110 22 132 25 131 18 128 17 100 23 112 22 E200 (vol% off) 45.7 44.7 52.5 51.4 46.6 48.5 53.1 57.7 45.5 44.1 51.0 50.9 E300 (vol% off) 81.5 79.0 83.3 81.3 81.8 81.3 84.2 83.5 80.0 79.9 82.2 83.5 Refinery Energy Use4Per Refinery Input (MM btu/b)5 0.49 0.44 0.43 0.55 0.51 0.49 0.60 0.53 0.52 

Per Refinery Output (MM btu/b)6 0.50 0.44 0.43 0.56 0.52 0.50 0.61 0.54 0.53 

1 Reported prices are for regular grade gasoline; ARMS marginal costs are for pool gasoline. 2 Wholesale/terminal price differential. ARMS differential assumes 5 octane number difference.3 Reported pool gasoline properties are based on EPA data for 2004 and CEC survey data for CARBOB in summer 2006.4 Reported data are for annual operations.5 Refinery inputs include crude oil, gas oils, and residuum.6 Refinery (net) outputs are light gases plus all other refined product outputs (except for coke): less the following refinery inputs: C4s, natural gas liquids, gasoline blendstocks, oxygenates, naphthas, and kerosene.Sources: Exhibits A-4, A-7, A-8, A-19, A-20a&b, C-2, C-3, C-4, and C-7.

October 8, 2010 
Single Octane NCG

Exhibit C-10a: Key Measures of Refinery Responses to NCG and Single Octane NCG Standards

Summer Season

PADD 1 PADD 2 PADD 3 C

Refer- 94 95 Refer- 94 95 Refer- 94 95 Refer- 

ence NCG RON RON ence NCG RON RON ence NCG RON RON ence NC

New Capacity & OperationsNew Capacity (K b/d)Hydrocracking 171 110 30 6Coking 18 24 24 27 37 46 55 63 127 142 167 191Alkylation 3 15 130 Pen/Hex Isomerization 36 200 142Reforming 16 46 40 CokingThroughput (K b/d) 98 104 104 106 335 343 351 358 1299 1313 1335 1357 405 4Fluid Cat CrackingThroughput (K b/d) 691 680 692 692 1,048 1,041 1,061 1,077 2,694 2,662 2,668 2,717 556 5Conversion 66.9 66.1 66.8 66.8 73.5 72.8 73.1 72.9 72.5 73.0 72.6 71.7 73.0 72HydrocrackingNaphtha Out-turns (%) 52.1 60.1 56.9 56.1 59.8 52.3 56.9 61.3 42.5 44.1 41.3 45.2 41.6 4ReformingCharge Rate (K b/d) 235 258 266 282 645 721 787 819 1,203 1,333 1,451 1,632 282 2Severity (RON) 96.0 96.9 100.1 100.7 94.8 94.8 97.7 100.5 97.3 97.7 100.3 101.0 91.7 9Inputs & Outputs (K b/d)Crude Oil 1,455 1,465 1,477 1,487 3,193 3,240 3,294 3,336 7,269 7,371 7,464 7,526 1,555 1,5Excessed MaterialC5s 6 14 27 37 25 114Coker Naphtha 

FCC Naphtha Gasoline Properties & OctaneOctaneRON 93.0 93.0 94.0 95.0 92.2 92.3 94.0 95.0 92.4 92.5 94.0 95.0 87.7 87MON 83.5 83.5 84.2 85.2 83.9 83.8 84.9 85.7 83.6 83.6 84.8 85.7 81.7 8CON 88.2 88.2 89.1 90.1 88.1 88.1 89.4 90.4 88.0 88.0 89.4 90.3 84.7 84Sensitivity (RON - MON)1 9.5 9.6 9.8 9.8 8.4 8.5 9.1 9.3 8.8 8.9 9.2 9.3 6.0 5

PropertyRVP (psi) 7.11 6.85 6.80 6.69 8.37 7.39 7.39 7.39 8.36 7.28 7.28 7.28 5.77 5Aromatics (vol%) 20.2 21.3 23.3 24.3 20.6 22.0 24.9 27.3 18.6 20.5 22.8 24.7 21.2 2Sulfur (ppm) 25 5 5 5 17 5 5 5 21 5558Estimated DI 1183 1189 1193 1203 1142 1159 1162 1165 1140 1150 1165 1187 1201 12Energy Density (MM btu/b) 5.077 5.086 5.095 5.099 5.032 5.059 5.075 5.086 5.028 5.060 5.065 5.087 5.216 5.2Gasoline Composition (%)C4s 1.5 1.0 1.0 0.9 3.5 1.7 1.8 1.9 2.8 1.2 1.3 1.9 1.1 Alkylate 11.5 11.5 11.8 13.0 12.2 12.3 12.2 12.2 13.6 13.7 13.8 16.5 17.5 18Isomerate 2.0 2.0 2.0 5.8 8.7 8.7 8.7 8.1 5.5 5.5 9.7 8.5 9.6 9Reformate 18.3 20.4 19.9 20.6 24.6 26.7 28.7 29.0 16.0 18.5 20.1 21.7 25.6 26Hydrocrackate 1.0 0.9 0.7 0.7 6.9 4.9 3.1 3.2 5.1 2.8 2.4 2.2 12.3 1FCC Naphtha 41.5 40.3 40.5 40.2 26.3 25.7 26.6 27.0 33.8 33.9 33.4 32.4 30.1 29All Other 24.2 24.0 24.1 18.8 17.9 20.1 18.9 18.7 23.2 24.4 19.2 16.7 3.8 4

1 Octane sensitivity for the California gasoline pool is less than 8 because we modeled CARBOB, not finished Calfornia RFG.

Otober 8, 2010 
Single Octane NCG

Exhibit C-10b: Key Measures of Refinery Responses to NCG and Single Octane NCG Standards

Winter Season

PADD 1 PADD 2 PADD 3 C

Refer- 94 95 Refer- 94 95 Refer- 94 95 Refer- 

ence NCG RON RON ence NCG RON RON ence NCG RON RON ence NC

New Capacity & OperationsCokingThroughput (K b/d) 83 86 87 88 311 311 315 318 1265 1268 1290 1292 402 4Fluid Cat CrackingThroughput (K b/d) 642 660 662 654 950 950 954 945 2,397 2,457 2,586 2,600 521 5Conversion 69.9 70.1 70.5 71.0 70.3 70.3 70.5 70.6 72.1 72.1 72.7 73.6 72.7 72HydrocrackingNaphtha Out-turns (%) 47.2 46.9 46.5 37.7 67.0 67.1 67.7 66.4 42.6 42.1 40.7 40.6 41.2 40ReformingCharge Rate (K b/d) 190 219 226 241 582 577 643 688 1,046 1,048 1,118 1,299 273 2Severity (RON) 94.8 94.2 98.7 100.2 92.6 93.3 97.7 100.6 97.5 96.8 100.3 100.6 91.7 9Inputs & Outputs (K b/d)Crude Oil 1,427 1,432 1,438 1,443 3,058 3,059 3,082 3,105 6,891 6,887 6,974 7,005 1,581 1,5Gasoline Properties & OctaneOctaneRON 92.8 92.7 94.0 95.0 92.1 92.1 94.0 95.0 92.0 92.0 94.0 95.0 87.7 87MON 83.7 83.7 84.7 85.6 84.0 84.0 85.6 86.4 84.0 84.0 85.5 86.3 81.5 8CON 88.2 88.2 89.4 90.3 88.1 88.1 89.8 90.7 88.0 88.0 89.8 90.6 84.6 84Sensitivity (RON - MON)1 9.1 9.0 9.3 9.4 8.1 8.0 8.4 8.6 8.0 8.0 8.5 8.7 6.2 6

PropertyRVP (psi) 12.00 12.00 12.00 12.00 13.72 13.72 13.72 13.72 11.88 11.88 11.88 11.88 10.03 10Aromatics (vol%) 17.6 16.8 18.7 19.9 16.9 17.1 20.1 22.4 16.2 15.9 18.3 19.9 20.2 20Sulfur (ppm) 25 5 5 5 16 5 5 5 19 5557Estimated DI 1076 1081 1083 1092 1041 1041 1041 1044 1055 1053 1065 1093 1113 11Energy Density (MM btu/b) 4.983 4.977 4.983 4.985 4.933 4.931 4.947 4.957 4.957 4.955 4.958 4.976 5.151 5.1Gasoline Composition (%)C4s 11.0 10.0 10.1 10.1 13.9 13.7 13.6 13.6 10.8 10.8 10.3 9.5 9.6 9Alkylate 8.7 9.5 10.1 10.3 9.9 10.0 10.2 10.6 12.9 13.3 13.4 15.9 10.1 10Isomerate 2.0 2.0 2.0 5.7 7.4 7.1 7.4 7.5 5.4 5.4 9.2 8.3 9.7 10Reformate 14.7 17.4 17.2 17.7 22.9 22.6 24.8 25.6 13.5 13.4 14.2 16.2 25.2 25Hydrocrackate 1.6 1.3 1.3 1.3 6.6 6.6 4.3 4.2 5.3 4.6 2.6 1.1 12.6 12FCC Naphtha 38.9 36.3 36.7 36.5 21.5 21.5 21.9 21.4 28.6 29.2 31.2 31.1 28.6 28All Other 23.2 23.4 22.6 18.4 17.8 18.4 17.8 17.1 23.4 23.3 19.1 17.9 4.1 4

1 Octane sensitivity for the California gasoline pool is less than 8 because we modeled CARBOB, not finished Calfornia RFG.

Otober 8, 2010