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Dispersion of Butane in Vapex: The Effect of Drainage Height

机译:丁烷在Vapex中的分散:排水高度的影响

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In this work, the dispersion of butane in heavy oil and bitumen is experimentally determined during the Vapexprocess with varying drainage heights. The experiments were performed at room temperature (22oC) using butane assolvent at the dew point pressure. We used cylindrical models with different heights varying from 15 to 45 cm, packedwith uniform mixture of heavy oil and glass beads. From the experiments, production rate dependency towards thedrainage height is evaluated along with determination of butane gas solubility, live oil density, and viscosity. Conjugategradient method is used to optimally determine concentration dependent dispersion coefficient as well as the solventconcentration at the solvent–oil interface by matching up experimental live oil production rates with ones predicted bymodel. A computational algorithm is developed to simultaneously solve process models of different heights, andoptimally determine the corresponding dispersion coefficients.
机译:在这项工作中,通过实验确定了Vapex过程中排水高度不同时丁烷在重油和沥青中的分散性。实验是在室温(22oC)下使用丁烷溶剂在露点压力下进行的。我们使用高度从15到45厘米不等的圆柱模型,里面装有重油和玻璃珠的均匀混合物。从实验中,可以评估生产率对排水高度的依赖性,并确定丁烷气体的溶解度,活油密度和粘度。共轭梯度法用于通过将实验活油的生产速率与模型预测的速率相匹配,来最佳地确定浓度依赖性分散系数以及溶剂-油界面处的溶剂浓度。开发了一种计算算法来同时求解不同高度的过程模型,并优化确定相应的色散系数。

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