摘要
考虑稠油(幂律流体)与稀油(牛顿流体)层间扩散、相间作用力、掺混粘度等参数,建立了掺稀采油管内牛顿-幂律流体的流速计算模型对其编程求解;从掺稀前及掺稀后两种工况着手,对稠油掺稀采油管内流速的径向分布规律进行了详细分析。结果表明:流速在油管中的分布呈现轴对称性;随采油管外径增大、稠油稠度系数增大及采油管压力降的减小,采油管径向上稠油流速呈现减小趋势;稠油掺稀过程中,与层流的流动对比分析发现,稠油和稀油掺混时紊流流动过程中的过渡段出现增大趋势,此时的掺混速度以及均匀程度都有所提高。
There is almost no existing studies focus on microscopic description of heavy oil and thin oil layer diffusion motion law. Thus, considering inter-layer diffusion, phase reaction, mixing viscosity parameters of heavy oil(power law fluid) and thin oil(Newtonian fluid), a Newton-power law fluid mixing flow velocity model is put forward. Through programming solution, radial distribution characteristics of flow velocity in tube and its mechanism between heavy oil and thin oil is discussed in detail by analyzing the two kinds of conditions, the blank heavy oil case and the diluted heavy oil case. The results show that the flow velocity in the tube isaxisymmetric. The radial distribution of heavy oil flow velocity in tube shows a trend of decreasing with the increase of borehole diameter, or decrease of pressure drop, or increase of viscosity of heavy oil. During the process of heavy oil diluted with thin oil, compared to laminar flow, the thickness of the transition section of heavy oil and thin oil increased when the flow in the tube is turbulent flow, so that the mixing speed and mixing uniformity can be improved.
引文
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