PRESSURE LOSS OF WATER–CO2 TWO-PHASE FLOW UNDER DIFFERENT OPERATING CONDITIONS

F. B. Rajeb, M. A. Rahman, Yan Zhang, S. Imtiaz, A. Aborig, Mohamed Odan
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Abstract

In the present study, pipe flows are used to investigate the behavior flow of water–CO2 mixtures at different pressures and temperatures. The flow rate and pressure of water and CO2 are changed by using a pump placed ahead of the mixing point. Pressure and temperature levels are recorded by pressure sensors and thermocouples affixed at points along the pipe loop. The flow regimes of two-phase water– CO2 flow is visualized through transparent tubes using a high-speed camera. After several experiments, it was found that the mean pressure drop along the tube for a water–CO2 system flow is about 4 kPa/m for water flow rates between 0.4 and 0.7 L/S and CO2 flow rates between 2.5 and 11 L/S. The maximum inlet pressure for water is 400 kPa and for CO2 is 3000 kPa. In this experiment, the phase fraction of water is approximately 0.5–0.15 and the phase fraction of CO2 is around 0.85–0.95. The investigated flow regime under these flow conditions is often intermittent.
不同工况下水- co2两相流压力损失
在本研究中,使用管道流动来研究水-二氧化碳混合物在不同压力和温度下的行为流动。水和二氧化碳的流速和压力是通过在混合点前面放置一个泵来改变的。压力和温度水平是由压力传感器和热电偶贴在点沿管道回路记录。利用高速摄像机通过透明管观察了水-二氧化碳两相流的流动状态。经过多次实验发现,当水流量为0.4 ~ 0.7 L/S, CO2流量为2.5 ~ 11 L/S时,水- CO2体系流沿管平均压降约为4 kPa/m。进水压力400kpa,二氧化碳压力3000kpa。在本实验中,水的相分数约为0.5-0.15,CO2的相分数约为0.85-0.95。在这些流动条件下所研究的流动形式通常是间歇性的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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