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* TABLE BUY

* Raw Material Purchases

TEXT MIN MAX FIX COST COST

* ('000 ('000 ('000 $/BBL $/Ton

* BPD) BPD) BPD)

* CRUDE OIL PURCHASES:ANS Alaskan N Slope 0.00000 33.00000 113.00000 828.29000NSF North Sea Forties 0.00000 20.00000 109.43000 802.12190TJL Tiajuana Light 0.00000 25.00000 104.11765 763.18235

*

ARL Arabian Light 20.00000 40.00000 104.80000 768.18400

AHV Arabian Heavy 0.00000 50.00000 95.75000 701.84750

MX1 Arabian Mix 0.00000 10.00000 100.27500 735.01575

BAC Bachequero 1.00000 8.00000 90.00000 659.70000

KUW Kuwait Export 0.00000 20.00000 100.23000 734.68590

*

* OTHER PURCHASES:

NC4 Normal Butane 0.00000 71.18000 810.90800

IC4 Iso-Butane 0.00000 73.91000C4m Mixed C4's 0.00000 61.40000

PGS Gas to H2 Plant, kscf 0.00000 0.00000***

CONVERSION FORMULA

1 barrel is equivalent to 0.159 m3

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API SPG ***

26.3900036.3300031.30000

33.8000027.22000 Convert Crude Prices to $/ton in the Yellow shaded cells30.51000 (Use the conversion formula given below)17.27000

35.09000

0.58440

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* TABLE CAPACITY

*

TEXT MIN MAX

* (BPD = Barrel Per Day)

CR01 Crude Processing

CR02 ====================

CAT1 Crude Unit #1 BPD 40000CAT2 Crude Unit #2 BPD 60000

CVT1 Vac Unit #1 BPD 20000

CVT2 Vac Unit #2 BPD 30000

CR03

CR04 Naphtha Processing

CR05 ====================

CNSP Naph Splitter BPD 27000

CNHT Naph Hydrotrt BPD 23000

CLPR Cat Reformer BPD 25000

CR06

CR07 Distillate Processing

CR08 ====================CKHT Kero Hydrotrt BPD 8000

CDHT Dist Hydrotrt BPD 0.50000 15000

CR09

CR10 Cracking

CR11 ====================

CCCU Cat Cracker BPD 17.00000 35000

CCRB Carbon Burnt TPD 300

CHCD Hydrocrack Dist BPD 5.00000 15000

CDLC Delayed Coker BPD 10.00000 20000

CR12

CR13 Other Processing

CR14 ====================

CIS4 C4 Isom BPD 5000CSFA Sulf Acid Alky BPD 12000

CHYD H2 Plant MMSCFD 600

CAMN Amine Unit LT/D 3000

CSRU Sulfur Plt LT/D 3000

CTGT Tail Gas Trt LT/D 200

CH2O Cooling Tower GPM

CSTM Steam Gen LB/HR 500000

CKWH Power Distrib KVA

***

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All data are in barrels per calendar day (b/cd) unless otherwise indicated.**Note: Analysis begins in column BW

Review all columns till Column CI

*Conversion rates used when refineries reported in barrels per stream day (b/sd)

are crude and vacuum .95, and all other units .90

Company Crude

Example refinery 90000

Refinery A 50000

Topping Refinery 50000

Hydroskimming Refinery 40000

Cracking RefineryA 30000

Cracking RefineryB 60000

Coking RefineryA 60000

Coking RefineryB 31300

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Thermal

Fluid Delayed Other Cracking Visbreaking Fluid

Vacuum (1) (2) (3) (1) (2) (1)

45000 25000 27500

25000 10000 12000

20000

20000 8000 12000

30000 10000

28900 10400 19000

18200 10850 10750

-------Coking------- ---Fresh

Thermal operations ---Cat Cr

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Distillate Residual

Other Semiregenerat Cyclic Continuous re Other Upgrading Upgrading

(2) (1) (2) (3) (4) (1) (2)

11500

13000 15000

5000

10000

12000 10000

12500 6200

6775

----Catalytic Hy

Feed--- --------Catalytic Reforming--------

acking---

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Pretreat. Other Naphtha Distillate

Lube Oil Cat Reformer Naptha Aromatics Kerosine/jet Diesel aromatics

Manufac. Other Feed Desulf. Saturation Desulf. Desulf. saturation

(3) (4) (1) (2) (3) (4) (5) (6)

20000 30000

13000 6000 8000

10000 5000 2000 10000

10000 9000

12000 10000 5000

13900 6600 10000

6775 2900 14700

drocracking-----

---------------------C

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Pretreatment Other

Other of cat cracker heavy gas oil Resid Lube oil Post hydrotreat

distillates feeds hydrotreating hydrotreating polishing of FCC naphtha Other

(7) (8) (9) (10) (11) (12) (13)

12000 6000

4000

7900 19200

3000 12880

atalytic Hydrotreating---------------------

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Sulfuric Hydrofluoric Polymer- Dimer- Hydrode- Cyclo-

Acid Acid ization ization BTX alkylation hexane

(1) (2) (1) (2) (1) (2) (3)

6000

2000 1800

3625

---------Aromatics-----------

---Alkylation--- Polymerization./Dimer.

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C4 C5 C5 & C6

Cumene Feed Feed Feed MTBE ETBE

(4) (1) (2) (3) Lubes (1) (2)

750

5000

1800

2000

----Isomerization---- ---------Oxyg

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Steam Steam Pressure

Methane Naphtha Partial Swing

TAME Other Reforming Reforming Oxidation Adsorption Cryogenic

(3) (4) (1) (2) (3) (4) (5)

enates---------

--------------------Hydrogen (MMcfd)----------------

----------Production: ----------R

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Membrane Other Coke Sulfur Asphalt

(6) (7) (8) (mt/d) (mt/d) (b/d)

8.48 120

0.3733 123

----

ecovery:

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Therm. Delayed Cat. Cat.

Crack. & Fluid Cat Cat. Hydro. Hydro.

Dist. Vac. Vis. Coking Crack. Reform. Crack. Refining a

1 2 2.75 6 6 5 6 2.5

90 45 25 0 27.5 11.5 0 50

50 25 0 10 12 13 15 27

50 0 0 0 0 0 0 0

40 20 0 0 0 5 0 17

30 20 8 0 12 10 0 19

60 30 10 0 0 12 10 27

60 28.9 0 10.4 19 12.5 6.2 30.5

31.3 18.2 0 10.85 10.75 6.775 0 24.375

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Alky. Aro.

d treating Poly. Iso. Lubes Asphlt. H2 Oxy Complexity

2.5 10 15 60 1.5 1.0 10.0 Index

0 0 0 0 0 0 0.75 6.7

0 6 5 0 0 0 0 11.8

0 0 0 0 0 0 0 1.0

10 0 0 0 0 0 0 4.3

18 2 3.6 0 0 0 0 12.7

4 0 0 0 0 0 0 5.8

27.1 0 0 0 0 0 0 9.0

15.88 3.625 2 0 0 0 0 12.7

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