Canadian Bitumen and Synthetic Crudes

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Understanding the Quality of Canadian Bitumen and Synthetic Crudes Pat Swafford Spiral Software Limited Crude Oil Quality Group Meeting February 26, 2009

Introduction Canadian crude production is increasing Canadian crudes have some unique characteristics that cause processing difficulties Refiners need to understand the quality issues in order to have success (both from a processing and economic standpoint) with Canadian crudes

Classes of Canadian Crude Oil Some of the commonly accepted classes of crudes produced in the Western Canadian Sedimentary Basin (WCSB) are as follows Condensate Light sweet crude Light sour crude Medium sweet crude Medium sour crude Heavy sour crude Synthetic crude

Heavy Sour Crude Production Volumetrically the largest classification of crudes produced in the WCSB Produced primarily from bitumen, most of them are blended to some extent The heavy sour crude class may be subdivided further into three categories: Conventional heavy sour Diluted bitumens (Dil-bits) Synthetic crude / bitumen blends (Syn-bits)

Conventional Heavy Sour Includes LLK, LLB and Bow River, among others These crudes tend to behave similarly to conventional heavy sour crudes produced in other regions of the world

Conventional Heavy Sour Yield Profile 100 Property Profile Graph 90 80 70 tive Yield (% vol) Cumulat 60 50 40 30 20 10 0-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200 Boiling Point ( F) CONVENTIONAL HEAVY CumYld(%v) 34 API BLEND CumYld(%v)

Dil-Bit Crudes Dil-bits are blends of heavy bitumen with a lighter diluent, typically Canadian condensate, to reduce the viscosity so that it may be transported throughout the pipeline system. Examples of Dil-bits include Cold Lake, Wabasca Heavy, and Peace Heavy. Diluent Bitumen Blending Dil-Bit

Heavy Sour Dil-bit Yield Profile 100 Property Profile Graph 90 80 70 tive Yield (% vol) Cumulat 60 50 40 30 20 10 0-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200 Boiling Point ( F) HEAVY-Dilbit CumYld(%v) 34 API BLE... CumYld(%v)

Syn-Bit Crudes Diluent Syn-bits are blends of heavy bitumen with a synthetic diluent. The Syn-bit category includes blends such as Christina Lake, Mackay River Heavy, and Surmont Heavy Blend. Bitumen Blendi ing Syn-Bit Western Canadian Select may also fall into this category, using both condensate and synthetic crude oil as diluent. Upgra ader Synthetic Crude

Heavy Sour Syn-bit Yield Profile 100 Property Profile Graph 90 80 70 ive Yield (% vol) Cumulat 60 50 40 30 20 10 0-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200 Boiling Point ( F) HEAVY-Synbit CumYld(%v) 34 API BLEND CumYld(%v)

Yield Profile of Heavy Sour Crude Naphtha Distillate VGO Residue Comment Conventional Crude (34 API) Heavy Sour Crude (22 API) % Difference from Conventional Crude 31.3 27.7 24.2 16.8 Lots of coker feed, 16.11 23.1 28.9 32 more FCC feed, less naphtha and distillate -48.6% -16.6% 19.4% 90.5%

Unique Characteristics of Heavy Sour Crude Yield Profile 100 Property Profile Graph 90 80 70 ive Yield (% vol) Cumulat 60 50 40 30 20 10 0-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200 Boiling Point ( F) HEAVY SOUR CRUDE CumYld(%v)

Synthetic Crude Production Produced in five major upgrading facilities in northwest Canada Upgrader Husky Primary Upgrading Process Coking, residue hydrocracking Syncrude Fluid coking, residue hydrocracking Shell (Scotford) Suncor NewGrade (Regina) Residue hydrocracking Delayed coking Residue hydrocracking

Typical Synthetic Crude Processing Scheme Hydrogen Manufacturing Process Diluent Bitumen Synthetic Crude Atmospheric Distillation Vacuum Distillation Hydrocracking Coking Hydrotreating Blending

Synthetic Crude Yield Profile 100 Property Profile Graph 90 80 70 tive Yield (% vol) Cumulat 60 50 40 30 20 10 0-200 0 200 400 600 800 1000 1200 1400 1600 1800 2000 2200 Boiling Point ( F) SYNTHETIC-Typical CumYld(%v) 34 API BLEND CumYld(%v)

Unique Characteristics of Synthetic Crude Yield Profile Naphtha Distillate VGO Residue Comment Conventional Crude (34 API) Synthetic Crude (33 API) % Difference from Conventional Crude 31.3 27.7 24.2 16.8 No coker feed, more 25.3 37.7 7 36.7 03 0.3 FCC feed, lotsof aromatic distillates -19.2% 36.1% 51.7% -98.2%

Unique Characteristics of Synthetic Crude Diesel Quality Synthetic crude 85 Cetane Index for Diesel (50 0-650F) 80 75 70 65 60 55 50 45 40 35 30 25 5 10 15 20 25 30 35 40 45 50 API for Crude (IBP-FBP)

Unique Characteristics of Synthetic Crude Jet Fuel Quality Synthetic crude (mm) for Kerosene (3 380-500F) 40 35 30 25 20 Smo oke Point ( 15 10 5 10 15 20 25 30 API for Crude (IBP-FBP) 35 40 45 50

Unique Characteristics of Synthetic Crude Sulfur Content Property / Property Scatter Graph 6 Synthetic crude 5 for Crude (IBP-FBP) hur (Total) (% wgt) f 4 3 2 Sulp 1 0 0 10 20 30 40 50 60 70 80 API (none) for Crude (IBP-FBP)

Using the Best Possible Assay Data to make Economic Decisions The ideal scenario would make accurate assay data available based on as-shipped quality The reality is that comprehensive assays are performed The reality is that comprehensive assays are performed only rarely and are never timely

Dealing with Assay Variability

Updating Heavy Sour Crude Assays Based on Injection Point Test Data Injection Point Test Data

Synthetic Crude Assays Synthetic crude quality tends to be fairly consistent Batch to batch, there is some variability in quality due to operational variations in the production facility. This results in the producer varying the amounts of the blendstocks that are used to produce the synthetic crude oil.

Dealing with Assay Variability

Updating Synthetic Crude Assays Based on Blend Components Synthetic Crude Blend Components

Replacing a Base Crude Slate with Canadian Crudes Refinery configurations are unique and typically geared toward a certain type of crude slate Some of the more challenging grades of Canadian Crudes cannot be processed in high percentages in a typical refinery Understanding the possible combinations of crudes and the acceptable amounts of each gives refinery planners and traders information that can be used to make economic decisions

Evaluating Blends of WCSB and Conventional Crudes Example PADD V Refinery A 3-way blend of the following constituents is assessed Alaskan North Slope Suncor Synthetic A Western Canadian Select The following quality constraints are set up in a Crude Approval Grid (CAG) for the blend: Sulfur content: desirable < 1.2 wt% Acidity: 0.5 mg KOH/g maximum Yield of naphtha fraction: < 22 vol% Yield of vacuum residue (coker feed): 10 18 vol%

Example Padd V Crude Approval Criteria

Crude Approval Grid Minimum ANS Minimum ANS

Crude Approval Grid Maximum ANS Maximum ANS

Crude Approval Grid Maximum OSA (with no WCS) Maximum OSA (with no WCS)

Conclusions Successful exploitation of West Canadian heavy crudes requires a good understanding of their qualities and how these interact with conventional crudes Spiral s advanced assay management tools enable this by Generating up-to-date assays of pipeline blends using batch testing data such as that available at CrudeMonitor.ca Evaluating blends with conventional crudes to match refinery constraints