欢迎登录材料期刊网

材料期刊网

高级检索

分别以牛顿流体和非牛顿流体为液相,研究了垂直管中零净液流量气液两相流的流动特性.提出了零净液流量气液两相流动模型,应用这一模型计算了零净液流量气液两相流的持液率和压力降,模型计算结果与试验结果相符.研究结果表明,零净液流量气液两相流与常规气液两相流相比具有特殊性,表现为其持液率仅由质量平衡方程控制,其摩擦阻力压力降为负值.

参考文献

[1] Turner R G;Hubbard M G;Dukler A E .Analysis and Prediction of Minimum Flow Rate for the Continuous Removal of Liquids from Gas Wells[J].Journal of Petroleum Technology,1969,21(11):1475-1482.
[2] Duncan R W;Scott S L.Vertical Zero Net Liquid Flow:Effects of High Pressure on Holdup[A].,1998:68-85.
[3] GregoryG;Scott D W .Correlation of Liquid Slug Velocity and Frequency in Horizontal Cocurrent Gas-Liquid Slug Flow[J].AICHE Journal,1969,16(06):933-935.
[4] Bendiksen K H .On the Motion of Long Bubbles in Vertical Tubes[J].International Journal of Multiphase Flow,1986,11(05):797-812.
[5] Taitel Y;Dukler A E .A Model for Predicting Flow Regime Transitions in Horizontal and Near Horizontal Gas-Liquid Flow[J].AICHE Journal,1976,22(01):47-55.
[6] Wallis G B.One-Dimensional Two-Phase Flow[M].New York: McGraw-Hill,1969
[7] Skelland A H P.Non-Newtonnian Flow and Heat Transfer[M].New York: John Wiley and Sons Inc,1967
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%