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Stability Analysis of Coupled Heat and Mass Transfer Boundary Layers During Steam-Solvent Oil Recovery Process

机译:蒸汽-溶剂油采收过程中传热传质边界层的稳定性分析

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摘要

Convective mixing at the edge of the steam chamber enhances heat and mass transfer rates, which increases oil mobility and production rate. A linear stability analysis is performed under transient concentration and steady-state temperature boundary layers with temperature and concentration dependent fluid density and viscosity. It is found that the critical Rayleigh number depends on coefficients of the mixture viscosity and density function. Results show that the onset of instability is delayed as the concentration and temperature dependency of the solvent-oil mixture viscosity increases. Different potential solvents for heavy oil recovery are compared based on the critical time of instability. It is shown that intermediate molecular weight solvents lead to stronger convection, which is in agreement with experimental observations reported in the literature. These results are applicable for optimum design of laboratory experiments and selection of appropriate additives to steam for design of field- scale heavy oil recovery process.
机译:蒸汽室边缘的对流混合提高了传热和传质速率,从而提高了油的流动性和生产率。在瞬态浓度和稳态温度边界层下进行线性稳定性分析,温度和浓度取决于流体密度和粘度。发现临界瑞利数取决于混合物粘度和密度函数的系数。结果表明,随着溶剂油混合物粘度的浓度和温度依赖性的增加,不稳定性的发生被延迟。根据不稳定性的临界时间比较了用于重油采收的不同潜在溶剂。结果表明,中等分子量的溶剂导致更强的对流,这与文献报道的实验观察结果一致。这些结果适用于实验室实验的优化设计,以及为现场规模的重油回收工艺设计选择合适的蒸汽添加剂。

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