期刊文献+

长庆油田川平46-23集输管路运行工况模拟研究

Simulation of the Operating Conditions of Chuanping 46-23 Gathering &Transporting Pipeline in Changqing Oilfield
下载PDF
导出
摘要 针对长庆油田川平46-23集输管路,利用管路的现场参数,通过对比分析优选出合适的流型划分模型、持液率模型、压降模型以及蜡沉积模型。对上述模型编程求解,分析了集输管路运行压力、温度、持液率、有效内径、气/液相表观流速、蜡沉积速率等随管道长度与运行时间的变化规律。模拟结果表明,在运行36h内,随管道长度的增加(除前60m),结蜡速率减小,压力降低,温度降低,气相表观流速增大,液相表观流速减小,持液率减小;随着运行时间的增加,同一节点处的蜡沉积速率增大,压力降低,温度升高,气、液相表观流速增大,持液率减小。 It is difficult to manage gathering & transportation pipelines because of their complicate operating conditions. Based on the Chuanping 46-23 gathering & transportation pipeline in Changqing oilfield and its operating parameters.The appropriate models,such as flow pattern model,liquid holdup calculation model,pressure drop calculation model and wax deposition model,were selected by comparative analysis.Then,the variation of operating pressure,temperature,liquid holdup,effective inner diameter,gas/liquid superficial velocity and wax deposition rate with pipe distance and operating time was analyzed by programming and calculating the models.The simulating results showed that the wax deposition rate, pressure,temperature,liquid superficial velocity and liquid holdup reduced,while gas superficial velocity increased with the increasing of pipeline length (except for the first 60 meters).The wax deposition rate,temperature,gas/liquid superficial velocity increases,the pressure and liquid holdup decreased at the same node with the increase of operating time within 36 operating hours.
出处 《石油化工高等学校学报》 CAS 2015年第5期78-84,共7页 Journal of Petrochemical Universities
基金 国家自然科学基金资助(51204202)
关键词 集输管路 模型优选 运行工况 模拟 Gathering and transportation pipeline Wax deposition Operating conditions Simulation
  • 相关文献

参考文献18

  • 1Xiao J, Shoham O, Brill J P. A comprehensive mechanistic model for two-phase flow in pipelines[D]. Tulsa:University of Tulsa, 1990.
  • 2Taitel Y, Dukler A E. A model for predicting flow regime transitions in horizontal and near horizontal gas-liquid flow [J]. AIChE Journal, 1976, 22(1): 47-55.
  • 3Barnea D. A unified model for predicting flow-pattern transitions for the whole range of pipe inclinations[J]. International Journal of Multiphase Flow, 1987, 13(1): 1-12.
  • 4Eaton B A, Knowles C R, Silberbrg I H. The prediction of flow patterns, liquid holdup and pressure losses occurring during continuous two-phase flow in horizontal pipelines [J]. Journal of Petroleum Technology, 1967, 19(6): 815-828.
  • 5Hughmark G A. Holdup and heat transfer in horizontal slug gas-liquid flow[J]. Chemical Engineering Science, 1965, 20 (12) : 1007-1010.
  • 6GHAbdul-Majeed. Liquid holdup in horizontal two phase gas-liquid flow[J]. Journal of Petroleum Science and Engineering, 1996(15): 271-280.
  • 7Eaton B A. The prediction of flow pattern, liquid holdup and pressure losses occurring during continuous two-phase in horizontal pipelines[J]. Journal of Petroleum Technology, 1967(6): 815-923.
  • 8喻西崇,赵金洲,冯叔初.起伏多相流管路持液率计算方法研究[J].西南石油学院学报,2000,22(3):94-97. 被引量:26
  • 9Mukherjee H, Brill J P. Liquid holdup correlations for incline two-phase flow [J]. Journal of Petroleum Technology, 1983(5) : 1003-1008.
  • 10Lockhart R W, Martinelli R C. Proposed correlations of data for isothermal two-phase, two-component flow in pipes [J]. Chem. Eng. Prog., 1949(45): 39.

二级参考文献12

  • 1Xiao J J,SPE2 0631,1990年,167页
  • 2冯叔初,油气集输,1988年
  • 3G H Abdul-Majeed.Liquid holdup in horizontal two-phasegas-liquid flow[ J ].JPSE,1996,(15) 271-280.
  • 4Eaton B A.The prediction of flowpattern,liquid holdup and pressure losses occurring during continuous two-phase in horizontal pipeliues[J].JPT,1967,(6):815 -923.
  • 5Hughmark G A.Holdup in gas-liquid flow[ J ].Chem Eng Prog,1962,(58):62.
  • 6Mukherjee,Brill.Liquid holdup correlations for Incline two-phase flow[J].JPT,1983(5):1003-1008.
  • 7Lockhart R W,Martinelli R C.Proposed correlations of data for isothermal two -phase,two-component flow in pipes[J].Chem Eng Prog,1949,(45):39.
  • 8Minami,Brill.Liquid holdup in wet-gas pipeline[ C ].SPE 14535,1988.
  • 9Xiao J J,Shpham O,Brill J P.A comprehensive mechanistic model for two-phase flow in pipelines[ C ].SPE20631,1990.
  • 10Dukler A E.Gas-liquid flow in pipelines[ R].Research Results,1969.

共引文献29

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