水平管气-液两相变质量流的均相流模型
Homogeneous Equilibrium Model for Gas-liquid Two-phase Flow in Horizontal Pipeline
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摘要: 与常规管中气-液两相流动不同, 水平管气-液两相变质量流动存在沿程管壁入流。在水平管单相变质量流动试验研究的基础上, 考虑了管壁入流对管壁摩阻系数的影响, 提出了孔缝管管壁摩阻系数相关式。将气-液两相混合物看作均匀介质, 使水平管气-液两相变质量流的均相流模型的基本模型等同于单相变质量流的流动模型, 重点研究了气-液两相变质量流均相流模型中流动参数的混合规则, 提出了新的气-液两相粘度混合规则。对气-液两相变质量流的均相流模型进行了试验验证, 研究结果表明, 气-液两相变质量流的均相流模型预测结果可以满足工程计算精度的要求。Abstract: Gas-liquid two-phase flow in horizontal porous pipe is different from gas-liquid two-phase flow in ordinary pipe, which includes wall inflow. Based on theory and experiment researches, a new correlation of wall friction factor for porous pipe flow with inflow is developed. In homogeneous equilibrium model, gas-liquid two-phase mixture is taken as homogeneous fluid. Therefore, the homogeneous equilibrium model for gas-liquid two-phase flow in horizontal porous pipe is the same as the model for single flow with mass transfer, only the flow parameters in homogeneous equilibrium model are taken as average values of two-phase mixture's homogeneous flow parameters. And the new correlation for mixture viscosity of gas- liquid two-phase fluid is developed. By experiment research, homogeneous equilibrium model for gas-liquid two-phase flow with mass transfer is validated. Its calculation accuracy meets the requirement of practical projects.