期刊文献+

胶凝原油试验管路的启动特性 被引量:8

Start-up characteristics of gelled crude oil test pipeline
原文传递
导出
摘要 针对胶凝原油管道停输后再启动压力远低于计算预测启动压力的技术难题,使用管流试验装置研究了胶凝原油管路的启动特性。依据对胶凝原油管道停输启动过程的理解,提出胶凝原油管道存在对应的临界启动剪切率和启动屈服应力。胶凝原油管路启动过程分为控制流量启动过程和控制压力启动过程。控制流量启动过程研究发现,受含蜡原油轻组分影响,试验管路内胶凝原油表现出"韧性"和"脆性"两种特性,"韧性"原油不含轻组分,胶凝结构强度与停输前的预剪切过程、停输静止时间、停输降温幅度、启动温度及启动剪切率相关;"脆性"原油含轻组分,胶凝结构强度主要取决于停输降温幅度和启动温度。胶凝原油的启动屈服应力取决于胶凝结构强度和静态降温过程的体积收缩;试验管路的启动速度与胶凝原油的结构强度和启动剪切率相关。控制压力启动过程研究发现,启动油温越高,试验管路全线启动速度越快;在相同启动油温下,启动压力越低,试验管路全线启动速度越慢;对应相同启动温度,存在临界启动压力。相关研究结果为深入研究胶凝原油停输再启动过程和指导工程实践奠定了理论基础。 Since the actual restart pressures in gelled crude oil pipelines after pipeline shutdown are much lower than the theoretical start-up pressures, the pipe flow test apparatus has been used to study start-up characteristics of such pipelines. With consideration to existing knowledge about the shutdown and start-up of gelled crude oil pipelines, critical start-up shear rates and start-up yield stresses corresponding to gelled crude oil pipelines have been proposed. The start-up procedure for gelled crude oil pipelines can be divided into two stages: start-up with control over flow rate and over pressure. By studying the start-up process with control over flow rate, it was found that gelled crude oil in the test pipeline is characterized by both "toughness" and "brittleness" due to the impact of lighter compositions in the waxy oil. Without lighter components, crude oil with "toughness" has gel structural strength closely related to pre-shearing procedure, shutdown duration, shutdown temperature drop, start-up temperature and start-up shear rate. At the same time, crude oil with lighter compositions and characterized by "brittleness" may have structural strength predominantly determined by shutdown temperature drop and start-up temperature. The start-up yield stress of gelled crude oil is determined by the structural strength and contraction in volume during static temperature drop. Start-up speed of the test pipeline is determined by structural strength and start- up shear rate of the gelled crude oil. By studying the start-up process with control over pressure, it was found that faster start-up speed can be obtained under higher start-up oil temperature. Under identical start-up oil temperatures, lower start- up pressure may lead to slower start-up speed of the pipeline. There are critical start-up pressures with the same start-up temperatures. Relevant research results provide theoretical basis for studying the shutdown and start-up process of gelled crude oil and guiding the engineering practice. (7 Figures, 10 Tables, 10 References)
作者 张国忠 刘刚
出处 《油气储运》 CAS 北大核心 2016年第7期734-741,共8页 Oil & Gas Storage and Transportation
基金 国家自然科学基金资助项目"胶凝原油管道启动问题中关键非定常参量研究" 51574274
关键词 胶凝原油 静态降温幅度 蜡晶结构恢复 启动温度 启动剪切速率 启动屈服应力 启动屈服面传递速度 gelled crude oil, static temperature drop, wax crystal structure recovery, start-up temperature, start-up shear rate, start-up yield stress, moving speed of start-up yield surface
  • 相关文献

参考文献5

二级参考文献38

  • 1蒋永兴.含蜡原油屈服过程及其受空隙影响的实验研究[J].力学与实践,1994,16(1):19-21. 被引量:6
  • 2张国忠,刘刚.大庆胶凝原油启动屈服应力研究[J].石油大学学报(自然科学版),2005,29(6):91-93. 被引量:21
  • 3孙长宇,陈光进,杨兰英,马昌峰.原油压缩系数实验与关联[J].化学工程,2006,34(2):29-32. 被引量:6
  • 4Sestak J,Charles M E,Cawkwell M G,et al. Start-up of gelled crude oil pipelines[J]. Journal of Pipelines, 1987,6:15- 24.
  • 5Cheng C,Nguyen Q D,Ronningsen H P. Isothermal start up of pipeline ttransporting waxy crude oil[J]. Journal of Non-Newto- nian Fluid Mechanics,1999,87:127- 154.
  • 6Vinay G,Wachs A, Agassant J F. Numerical simulation of non-i- sothermal viscoplastic waxy crude oil flows[J]. Journal of Non- Newtonian Fluid Mechanics ,2005,128 : 144-162.
  • 7Cawkwell M G,Charles M E. An improved model for start-up of pipelines containing gelled crude oil [J]. Journal of Pipelines, 1987,7:41-52.
  • 8Davidson M R,Nguyen Q D,Cheng C,et al. A model for restart of a pipeline with compressible gelled waxy crude oil[J]. Journal of Non-Newtonian Fluid Mechanics, 2004,123 : 269-280.
  • 9Vinay G, Wachs A, Frigaard I. Start-up transients ancl efficient computation of isothermal waxy crude oil flows[J]. Journal of Non-Newtonian Fluid Mechanics, 2007,143 : 141-156.
  • 10Wachs A,Vinay G,Frigaard I. A 1.5D numerical model for the start up of weakly compressible flow of a viscoplastie and thixo- tropic fluid in pipelines[J]. Journal of Non-Newtonian Fluid Me- chanics,2009,159 : 81-94.

共引文献36

同被引文献58

引证文献8

二级引证文献12

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