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在本实验参数范围内可将孔隙流道内空气/水两相流动划分为泡状流、泡状一弹状混合流、弹状流、弹状一环状混合流和环状流五种流型.本文修正后的Tung/Dhir流型转变模型与实验符合较好.依据单相流动压降数据,对Ergun公式参数进行了拟合,提出了适用于本实验特点的单相压降公式.并在此基础上利用渗透率系数提出了两相流动压降计算经验公式,与前人的公式相比,适用范围更广,计算误差也较小.

参考文献

[1] Schmidt W .Interfacial drag of two-phase flow in porous media[J].International Journal of Multiphase Flow,2007(6):638-657.
[2] Nemec D;Levec J .Flow through packed bed reactors: 2. Two-phase concurrent downflow[J].Chemical Engineering Science,2005(24):6958-6970.
[3] M. Jamialahmadi;H. Mueller-Steinhagen;M.R. Izadpanah .Pressure drop, gas hold-up and heat transfer during single and two-phase flow through porous media[J].International journal of heat and fluid flow,2005(1):156-172.
[4] Alessio Alexiadis .Bubble dispersion patterns in bubbly-flow released from a porous plug into a gas-stirred ladle[J].Applied mathematical modelling,2007(8):1534-1547.
[5] B. Eisfeld;K. Schnitzlein .The influence of confining walls on the pressure drop in packed beds[J].Chemical Engineering Science,2001(14):4321-4329.
[6] Nemec D;Levec J .Flow through packed bed reactors: 1. Single-phase flow[J].Chemical Engineering Science,2005(24):6947-6957.
[7] Attou A. .Modelling of the hydrodynamics of the cocurrent gas-liquid trickle flow through a trickle-bed reactor[J].Chemical Engineering Science,1999(6):785-802.
[8] Damjan Nemec;Gorazd Bercic;Jannez Levec .The hydrodynamics of trickling flow in packed beds operating at high pressures .The relative permeability concept[J].Chemical Engineering Science,2001(21/22):5955-5962.
[9] Ana Lakota;Janez Levec;Ruben G.Carbonell .Hydrodynamics of trickling flow in packed beds: relative permeability concept[J].AIChE Journal,2002(4):731-738.
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