刘振江, 张伟明, 郭芮. 管道气顶排空过程的压降计算方法[J]. 油气储运, 2016, 35(12): 1306-1313. DOI: 10.6047/j.issn.1000-8241.2016.12.010
引用本文: 刘振江, 张伟明, 郭芮. 管道气顶排空过程的压降计算方法[J]. 油气储运, 2016, 35(12): 1306-1313. DOI: 10.6047/j.issn.1000-8241.2016.12.010
LIU Zhenjiang, ZHANG Weiming, GUO Rui. A calculation method on the pressure drop in the process of gas-displacing-oil pipeline emptying[J]. Oil & Gas Storage and Transportation, 2016, 35(12): 1306-1313. DOI: 10.6047/j.issn.1000-8241.2016.12.010
Citation: LIU Zhenjiang, ZHANG Weiming, GUO Rui. A calculation method on the pressure drop in the process of gas-displacing-oil pipeline emptying[J]. Oil & Gas Storage and Transportation, 2016, 35(12): 1306-1313. DOI: 10.6047/j.issn.1000-8241.2016.12.010

管道气顶排空过程的压降计算方法

A calculation method on the pressure drop in the process of gas-displacing-oil pipeline emptying

  • 摘要: 为了完善机动管道气液两相流的压降计算方法,为管道充气排液的设计提供理论依据,介绍了基于流型的水平管气液两相流压降计算方法,回顾总结了流型的划分方式,提出了流型划分中存在的问题;对均相流模型、飘移流模型、分相流模型进行了对比,介绍了有代表性的和近几年出现的与流型相关的压降计算方法;分析了机动管道充气排液工况中的常见流型以及流型和压降的变化趋势,排空的初始阶段为分层流,排空中间阶段分层流和段塞流同时存在,排空的最后阶段出现短暂的环状流。将排空管道分为纯气体段、气液混合段及纯液体段,建立了不同工况下的压降模型,并提出了机动管道气顶油排空中亟需解决的问题。

     

    Abstract: This paper is aimed at improving the pressure-drop calculation method of gas-liquid two-phase flow in mobile pipeline and providing the theoretical basis for the design of gas-displacing-oil pipeline emptying. Firstly, the pressure-drop calculation methods of gas-liquid two-phase flow in horizontal pipe based on flow pattern were introduced. Secondly, the classification of flow pattern was reviewed and summarized and the existing problems related to the classification were pointed out. Thirdly, homogeneous flow model, drift flow model and separated flow model were compared and some typical or recently developed pressure drop calculation methods related to flow pattern were described. Fourthly, the common flow patterns and the evolutional trend of flow pattern and pressure drop in the process of gas displacing oil in mobile pipelines were analyzed. It is stratified flow at the initial stage of pipeline emptying, stratified flow and slug flow simultaneously at the intermediate stage and temporary annular flow at the final stage, and accordingly the pipeline is divided into pure gas section, gas-liquid mixed section and pure liquid section. Finally, the pressure-drop model for different operational modes was established and the urgent problems related to gas-displacing-oil mobile pipeline emptying were pointed out.

     

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