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Two-phase factional pressure drop of gas-non-Newtonian liquid flow through helical coils in vertical orientation

机译:气体-非牛顿液体在垂直方向上通过螺旋线圈的两相分流压降

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Investigations have been carried out to evaluate the two-phase frictional pressure drop for gas-non-Newtonian liquid flow through helical coils in vertical orientation.The experiments performed using nine coils and four different non-Newtonian liquids.The effects of gas and liquid flow rate,coil diameter,and liquid properties on two-phase frictional pressure drop have been illustrated.An attempt has been made to fit the experimental two-phase frictional pressure drop data by the Lockhart and Martinelli[R.W.Lockhert,R.C.Martinelli,Proposed correlation of data for isothermal two-phase two components flow in pipes,Chem.Eng.Prog.45(1949)39-48]correlation and the modified Lockhart-Martinelli correlation as presented by different authors.In another approach,friction factor method was adopted to correlate the experimental data by dimensional analysis.The correlation developed predicts the two-phase frictional pressure drop with acceptable statistical accuracy.
机译:进行了研究以评估非牛顿气体在垂直方向上通过螺旋形盘管的两相摩擦压降,使用9个盘管和四种不同的非牛顿液体进行了实验。示出了两相摩擦压降的速率,盘管直径和液体性质。洛克哈特和马丁内利[RWLockhert,RCMartinelli,建议的相关性]试图拟合实验的两相摩擦压降数据。管道中的等温两相两组分流动数据,化学工程(45)(1949)39-48)相关性和不同作者提出的改进的洛克哈特-马丁尼利相关性。另一种方法是采用摩擦系数法通过尺寸分析将实验数据关联起来。建立的关联性可以预测出两相摩擦压降,并且具有可接受的统计精度。

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