期刊文献+

油气水三相段塞流与滚动波流型的转变 被引量:2

Transition from slug flow to roll wave flow in oil-gas-water three-phase horizontal pipe
下载PDF
导出
摘要 Compared with gas-liquid two-phase flow,oil-gas-water three-phase flow is much more complex.There is immiscible oil-water,whose interaction and dispersion greatly affects the flow characteristics.The slug flow pattern of oil-gas-water three-phase and its flow pattern transition were studied in a 95 m long,51 mm i.d.horizontal pipe.The oil-gas-water three-phase slug flow pattern could be classified into five sub-flow patterns.The slug flow was W/O or O/W one during its transition to roll wave,which was three-layer flow pattern without mixed-phase on the interface.An even larger superficial gas velocity was needed for the transition boundary of slug flow and roll wave flow when the superficial liquid velocity is large.Besides,the region of roll wave flow pattern became smaller.The above-mentioned transition only happened when the water cut of liquid was between 30% and 70%.At the same superficial liquid velocity,there appeared a minimum superficial gas velocity corresponding to the transition of flow pattern when the water cut of liquid was between 40% and 50%. Compared with gas-liquid two-phase flow,oil-gas-water three-phase flow is much more complex.There is immiscible oil-water,whose interaction and dispersion greatly affects the flow characteristics.The slug flow pattern of oil-gas-water three-phase and its flow pattern transition were studied in a 95 m long,51 mm i.d.horizontal pipe.The oil-gas-water three-phase slug flow pattern could be classified into five sub-flow patterns.The slug flow was W/O or O/W one during its transition to roll wave,which was three-layer flow pattern without mixed-phase on the interface.An even larger superficial gas velocity was needed for the transition boundary of slug flow and roll wave flow when the superficial liquid velocity is large.Besides,the region of roll wave flow pattern became smaller.The above-mentioned transition only happened when the water cut of liquid was between 30% and 70%.At the same superficial liquid velocity,there appeared a minimum superficial gas velocity corresponding to the transition of flow pattern when the water cut of liquid was between 40% and 50%.
出处 《化工学报》 EI CAS CSCD 北大核心 2010年第3期629-634,共6页 CIESC Journal
基金 国家高技术研究发展计划项目(2006AA09Z302)~~
关键词 段塞流 滚动波 流型 转变边界 水平管 slug flow roll wave flow pattern transition boundary horizontal pipe
  • 相关文献

参考文献16

  • 1Nuland S. Phase fraction in three phase gas/oil/water flow//Proc. 5th Int. Conf. on Multiphase Flow. Cannes, France, 1991.
  • 2Acikgoz M, Lahey R T. An experiment study of three -phase flow regimes. Int. J. MultiphaseFlow, 1992, 18 (3): 327- 336.
  • 3Lee A H, Jepson W P. Study of flow regime of transition oil/water/gas mixtures in horizontal pipelines//Proc. 3rd Int. Offshore and Polar Eng. Conf. Singapore, 1993.
  • 4Hewitt G F, Pan I., Khor A H. Three phase gas liquid liquid flow: flow pattern, holdup and pressure drop. ISMF, 1997, 97: 7-10.
  • 5Arirachakaran S, Oglesby K D, Malinowsky M S. An analysis of oil/water flow phenomena in horizontal pipes. SPE 18836, 1989.
  • 6Lahey R T, Acikgoz M, Franca F. Global volumetric phase fractions in horizontal three phase flows. AIChE J. ,1992, 38 (7): 389 -397.
  • 7Stapelberg H, Mews D. Pressure drop calculation in three phase slug flow of water, oil and air. Int. Chem. Eng. , 1994, 34 (3): 295 -314.
  • 8Tronconi E. Prediction of slug frequency in horizontal two- phase slug flow. AIChEJ. , 1990, 36 (5): 701- 709.
  • 9Pan L, Jayanti S, Hewitt G F. Flow pattern, phase inversion and pressure gradient of air oil water flow in a horizontal pipe//Proc. 2nd Int. Conf. Multiphase Flow. Kyoto, Japan, 1995.
  • 10Nadler M, Mews D. The pressure drop of the three phase flow of oil, water, and gas in horizontal pipes//Proc. 2nd Int. Conf. Muhiphase Flow. Kyoto, Japan, 1995.

二级参考文献15

  • 1赵庆军,何利民,徐建中.水平管段塞流压力/压差波动特性分析[J].工程热物理学报,2005,26(3):441-446. 被引量:8
  • 2罗小明,何利民,王海琴.下倾管中活塞流液塞长度波动特性[J].化工学报,2006,57(3):536-540. 被引量:2
  • 3罗小明,何利民,陈振瑜.下倾管中段塞流液塞长度波动的非线性分析[J].高校化学工程学报,2006,20(5):702-706. 被引量:3
  • 4Nishikawa K, Sekoguchi K, Fukano T. On the pulsation phenomena in gas liquid two phase flow ( relationship Between pulsating pressure and flow pattern in upward two phase flow). JSME Bulletin, 1969, 12: 1410- 1416
  • 5Weisman J, Duncan D, Gibson J, Crawford T. Effects of fluid properties and pipe diameter on two phase flow patterns in horizontal lines. Int. J. Multiphase Flow, 1979, 5: 437 -462
  • 6Franca F, Acikgoz M, Lahey R T, Clausse A. The use of fractal techniques for flow regime identification. Int. J. MultiphaseFlow, 1991, 17: 545- 552
  • 7Kozma R, Kok H, Sakuma M, Djainal D D, Kitamura M. Characterization of two-phase flows using fractal analysis of local temperature fluctuations. Int. J. Multiphase Flow, 1996, 22: 953-968
  • 8Wu Haojiang, Zhou Fangde, Wu Yuyuan. Intelligent identification system of flow regime of oil gas water multiphase flow. Int. J. Multiphase Flow, 2001, 27: 459-475
  • 9Nydal O J, Pintus S, Andreussi P. Statistical characterizations of slug flow in horizontal pipes. Int. J. Multiphase Flow, 1992, 18:439 -453
  • 10Saether G, Bendiksen K, Muller J, Froland E. The fractal statistics of liquid slug lengths, lnt. J. Multiphase Flow, 1990, 16:1117 -1126

共引文献11

同被引文献7

引证文献2

二级引证文献3

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部