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Measurements of Molecular Diffusion Coefficients of Carbon Dioxide and Methane in Heavy Oil

机译:重油中二氧化碳和甲烷分子扩散系数的测量

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Heavy oil and bitumen reserves in Western Canada are of great economic importance. An efficient heavy oil recovery from these reserves requires significant reduction in heavy oil viscosity. Recent studies focus on vapor extraction (VAPEX) and other solvent-based processes, which are considered as promising heavy oil recovery techniques. In order to design a solvent-based EOR operation, one needs to know the rate and extent of oil mobilization by solvent. This requires the knowledge of molecular diffusion coefficient of solvent gas in heavy oil. Among the existing experimental methods for measuring the diffusivity, in this paper, the so-called pressure decay method is employed to measure the molecular diffusivity of a gas solvent in heavy oil by monitoring the decaying pressure. In this non-intrusive method, physical contact of gas solvent and heavy oil is made and thereby the pressure vs. time data are measured until the heavy oil reaches its complete saturation. With the measured data and a mathematical model for diffusion process, the diffusion coefficient is determined. Specifically, the molecular diffusion coefficients of carbon dioxide-heavy oil and methane-heavy oil systems are measured. The experiment is conducted in a closed high-pressure cell at constant reservoir temperature. Furthermore, the mathematical modeling is undertaken to obtain the analytical solution to the bulk diffusion equation subjected to appropriate boundary conditions at the solvent-heavy oil interface for each solvent. In terms of conservation law of mass and the equation of state for a real gas, the pressure in the gas phase is predicted from the analytical solution. Thus, solvent diffusivity is determined by finding the best match of the numerically predicted pressures with the experimentally measured pressures. The simultaneous search method is adopted in the numerical scheme. Finally, such obtained diffusion coefficients are compared with the limited data available in the literature.
机译:加拿大西部重油和沥青储量具有很大的经济意义。这些储备的高效较高的油恢复需要重大粘度的显着降低。最近的研究专注于蒸汽提取(VAPEX)和其他基于溶剂的方法,被认为是具有很强的重油回收技术。为了设计基于溶剂的EOR操作,需要了解溶剂的速率和程度。这需要了解重油中溶剂气体的分子扩散系数。在用于测量扩散率的现有实验方法中,本文采用所谓的压力衰减方法来通过监测衰减压力来测量重油中的气体溶剂的分子扩散性。在这种非侵入式方法中,制备气体溶剂和重油的物理接触,从而测量压力与时间数据,直到重油达到完全饱和。利用测量的数据和用于扩散过程的数学模型,确定扩散系数。具体地,测量二氧化碳重油和甲烷重油系统的分子扩散系数。该实验在恒定的储液温度下在封闭的高压电池中进行。此外,进行数学建模,以获得对每个溶剂的溶剂重油界面上对散装扩散方程的分析溶液进行分析溶液。在质量保守规律和实际气体的状态方程方面,从分析溶液预测气相中的压力。因此,通过在实验测量的压力下找到数值预测压力的最佳匹配来确定溶剂扩散性。在数值方案中采用同时搜索方法。最后,将这种获得的扩散系数与文献中可用的有限数据进行比较。

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