两相液气流动在锐边孔口压降的数值与机理模拟

Zurwa Khan, R. Tafreshi, M. Franchek, K. Grigoriadis
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摘要

在石油、化工和核工业中,两相液气流动的孔间压降估算对于阀门和管道的尺寸以及降低不安全后果或高成本的可能性至关重要。虽然通过孔板流动的数值模拟是一项复杂的任务,但它可以评估许多孔板设计和操作参数的影响。本文采用数值模拟方法研究了不同流体组合和不同孔板几何形状对压降的影响。假设孔板位于上游和下游流动完全发达的管道中。在表面速度为10 m/s的条件下,研究了两种液-气流体组合,即水-空气和汽油-液-气混合物,其孔板与管道的面积比为0.01 ~ 1。采用流体体积多相流模型和k-epsilon湍流模型对管道内液气混合物的压力分布进行了估计。对水-空气模型进行了验证,平均相对误差小于10.5%。正如预期的那样,由于孔板组件的收缩系数增加,孔板与管道面积比的降低导致了更大的压降。由于孔口下游形成较大的涡流,水-空气相对于汽油混合物具有较大的压降。同时,建立了直接估计孔间局部两相压降的力学模型。利用Woldesemayat和Ghajar的相关性预测了气含率,并将其应用于由于孔口而经历收缩和膨胀的分离两相流。模型结果在不同孔口和流速下进行了验证,总体相对误差小于40%,由于测量实验压降的不确定性,这是可以接受的。所建立的数值模型与力学模型的比较表明,数值模型能够达到较高的精度,而力学模型的计算量最少。
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Numerical and Mechanistic Modelling of Two-Phase Liquid-Gas Flow’s Pressure Drop Across Sharp-Edged Orifices
Pressure drop estimation across orifices for two-phase liquid-gas flow is essential to size valves and pipelines and decrease the probability of unsafe consequences or high costs in petroleum, chemical, and nuclear industries. While numerically modeling flow across orifices is a complex task, it can assess the effect of numerous orifice designs and operation parameters. In this paper, two-phase flow across orifices has been numerically modeled to investigate the effect of different fluid combinations and orifice geometries on pressure drop. The orifice is assumed to be located in a pipe with fully-developed upstream and downstream flow. Two liquid-gas fluid combinations, namely water-air, and gasoil liquid-gas mixture were investigated for different orifice to pipe area ratios ranging from 0.01 to 1 for the superficial velocity of 10 m/s. Volume of Fluid multiphase flow model along with k-epsilon turbulence model were used to estimate the pressure distribution of liquid-gas mixture along the pipe. The numerical model was validated for water-air with mean relative error less than 10.5%. As expected, a decrease in orifice to pipe area ratio resulted in larger pressure drops due to an increase in the contraction coefficients of the orifice assembly. It was also found that water-air had larger pressure drops relative to gasoil mixture due to larger vortex formation downstream of orifices. In parallel, a mechanistic model to directly estimate the local two-phase pressure drop across orifices was developed. The gas void fraction was predicted using a correlation by Woldesemayat and Ghajar, and applied to separated two-phase flow undergoing contraction and expansion due to an orifice. The model results were validated for different orifices and velocities, with the overall relative error of less than 40%, which is acceptable due to the uncertainties associated with measuring experimental pressure drop. Comparison of the developed numerical and mechanistic model showed that the numerical model is able to achieve a higher accuracy, while the mechanistic model requires minimal computation.
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