泡沫流体管流流动与换热数值模拟

基于质量、动量和能量守恒方程,建立泡沫流体在圆管内流动与换热的物理模型和数学模型,并利用FLUENT软件进行模拟,得到不同雷诺数下圆管内的压力损失、管道横截面上的速度分布和表观黏度分布,同时回归了不同雷诺数下的摩阻系数和努塞尔数经验关系式。结果表明:管内压力沿管程不断降低,且流速越大压降越大;管内温度沿管程不断升高,且流速越小温升越大;管道横截面上的速度、温度分布不均匀,越接近管壁速度越小,温度越高。

垂直管中气-水-泡沫三相管流空隙率实验研究

空隙率是计算气-水-泡沫三相管流压力、温度的重要参数,准确预测气井中气-水-泡沫三相管流空隙率对泡沫排水采气工艺技术的高效实施及方案优化至关重要。目前关于气-水两相管流空隙率模型研究较多,而气-水-泡沫空隙率研究相对薄弱。因此通过开展气-水-泡沫三相空隙率测量实验,研究了泡排剂浓度、气量、液量对空隙率大小的影响规律。基于漂移模型,考虑泡排剂浓度、气液表观流速、密度、滑脱速度等参数,建立了适用于垂直管的气-水-泡沫三相管流空隙率模型,并分别利用145组实验数据和602组文献数据验证了模型的准确度。结果表明,预测实验数据时平均相对误差为2.24%,平均绝对误差为2.47%;预测文献时平均相对误差为-4.65%,平均绝对误差为6.21%;证明新模型计算精度较高,可满足工程需求。新模型可为泡沫排水采气工艺技术的高效实施和方案优化提供理论指导。

Investigation of Heat Transfer of Tube Line of Staggered Tube Bank in TwoPhase Flow

This article presents the results of experimental investigation of heat transfer process, carded out using the model of heat exchanger. Two-phase statically stable foam flow was used as a heat transfer fluid. Heat exchanger model consisted of staggered tube bank. Experimental results are presented with the focus on influence of tube position in the line of the bank, volumetric void component and velocity of gas component of the foam. The phenomena of liquid draining in cellular foam flow and its influence on heat transfer rate has also been discussed. The experi- mental results have been generalized by relationship between Nusselt, Reynolds and Prandtl numbers.