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Toe-to-Heel Air Injection (THAI) is a variant of conventional In-Situ Combustion (ISC) that uses a horizontal production well to recover mobilised partially upgraded heavy oil. It has a number of advantages over other heavy oil recovery techniques such as high recovery potential. However, existing models are unable to predict the effect of the most important operational parameters, such as fuel availability and produced oxygen concentration, which will give rise to unsafe designs. Therefore, we have developed a new model that accurately predicts dynamic conditions in the reservoir and also is easily scalable to investigate different field scenarios. The model used a three component direct conversion cracking kinetics scheme, which does not depend on the stoichiometry of the products and, thus, reduces the extent of uncertainty in the simulation results as the number of unknowns is reduced.The oil production rate and cumulative oil produced were well predicted, with the latter deviating from the experimental value by only 4%. The improved ability of the model to emulate real process dynamics meant it also accurately predicted when the oxygen was first produced, thereby enabling a more accurate assessment to be made of when it would be safe to shut-in the process, prior to oxygen breakthrough occurring. The increasing trend in produced oxygen concentration following a step change in the injected oxygen rate by 33 % was closely replicated by the model. The new simulations have now elucidated the mechanism of oxygen production during the later stages of the experiment.The model has allowed limits to be placed on the air injection rates that ensure stability of operation.Unlike previous models, the new simulations have provided better quantitative prediction of fuel laydown, which is a key phenomenon that determines whether, or not, successful operation of the THAI process can be achieved. The new model has also shown that, for completely stable operation, 2 2 the combustion zone must be restricted to the upper portion of the sand pack, which can be achieved by using higher producer back pressure.
Toe-to-Heel Air Injection (THAI) is a variant of conventional In-Situ Combustion (ISC) that uses a horizontal production well to recover mobilised partially upgraded heavy oil. It has a number of advantages over other heavy oil recovery techniques such as high recovery potential. However, existing models are unable to predict the effect of the most important operational parameters, such as fuel availability and produced oxygen concentration, which will give rise to unsafe designs. Therefore, we have developed a new model that accurately predicts dynamic conditions in the reservoir and also is easily scalable to investigate different field scenarios. The model used a three component direct conversion cracking kinetics scheme, which does not depend on the stoichiometry of the products and, thus, reduces the extent of uncertainty in the simulation results as the number of unknowns is reduced.The oil production rate and cumulative oil produced were well predicted, with the latter deviating from the experimental value by only 4%. The improved ability of the model to emulate real process dynamics meant it also accurately predicted when the oxygen was first produced, thereby enabling a more accurate assessment to be made of when it would be safe to shut-in the process, prior to oxygen breakthrough occurring. The increasing trend in produced oxygen concentration following a step change in the injected oxygen rate by 33 % was closely replicated by the model. The new simulations have now elucidated the mechanism of oxygen production during the later stages of the experiment.The model has allowed limits to be placed on the air injection rates that ensure stability of operation.Unlike previous models, the new simulations have provided better quantitative prediction of fuel laydown, which is a key phenomenon that determines whether, or not, successful operation of the THAI process can be achieved. The new model has also shown that, for completely stable operation, 2 2 the combustion zone must be restricted to the upper portion of the sand pack, which can be achieved by using higher producer back pressure.
The article contains sections titled: 1. Introduction 2. Definitions 3. Chemistry 4. Viscous Oil Origins, Geological Setting and Resource Base Estimates 4.1. Viscous Oil Origins 4.2. Geographical Distribution and Resource Base Estimates 4.3. Canadian Oil Sands Deposits 4.3.1. The Athabasca Oil Sands 4.3.2. The Cold Lake Oil Sands 4.3.3. The Peace River Viscous Oil Sands 4.3.4. The Wabiskaw Viscous Oil Sands 4.3.5. The Heavy Oil Belt 4.3.6. Venezuelan Viscous Oil Deposits 4.4. Other Major Viscous Oil Deposits 4.4.1. Russia 4.4.2. Kazakhstan 4.4.3. Kuwait 4.4.4. China 4.4.5. Iran 5. In situ Production Technologies 5.1. Historical Development 5.2. Surface Mining 5.3. New Oil Production Technologies 5.3.1. Technical Screening Criteria for VO Production 5.3.2. VO Production Cost Estimates 5.3.3. Nonthermal Commercialized Methods 5.3.3.1. Cold Production 5.3.3.2. Cold Heavy Oil Production With Sand 5.3.3.3. Pressure Pulse Stimulation Technology 5.3.4. Commercialized Thermal Methods 5.3.4.1. In Situ Combustion 5.3.4.2. Conventional Steam Processes 5.3.4.3. Vertical Well Cyclic Steam Stimulation 5.3.4.4. Horizontal Well Cyclic Steam Stimulation 5.3.4.5. Steam Assisted Gravity Drainage 5.3.5. Emerging Methods 5.3.5.1. Vapor‐Assisted Petroleum Production 5.3.5.2. Toe‐to‐Heel‐Air Injection 5.3.5.3. CAPRI 5.3.5.4. Deep Miscible CO 2 Injection 5.3.6. Hybrid Approaches and Sequencing of Technologies 5.3.7. Geomechanics of Thermal VO Production 5.3.8. Steam Generation 5.3.9. Further Technical Issues 6. Upgrading and Transportation 6.1. Noncatalytic Processes in VO Upgrading 6.1.1. Solvent Deasphaltening 6.1.2. Thermal Conversion 6.1.2.1. Gasification 6.1.2.2. Delayed Coking 6.1.2.3. Fluid Coking and Flexicoking 6.1.2.4. Visbreaking 6.2. Catalytic Processes in VO Upgrading 6.2.1. Fluid Catalytic Cracking 6.2.2. Hydroprocessing/Hydrogenation 6.3. Hydrogen Sources 6.4. Coke 6.5. Sulfur Removal 6.6. Future Developments in Upgrading 6.7. Viscous Oil Transportation 7. Environmental Issues 7.1. Surface Mining Solid Wastes 7.2. Surface Mining Liquid Wastes and Sludges 7.3. In Situ Viscous Oil Recovery Processes 7.4. Sulfur and Coke 7.5. General Waste Management Options 7.6. Zero Emissions Targets 7.7. Greenhouse Gas Emissions 7.8. Water Issues
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