邓志安, 刘丹丹. CO2驱采出液分离器内构件分离特性数值模拟[J]. 油气储运, 2017, 36(6): 722-727. DOI: 10.6047/j.issn.1000-8241.2017.06.017
引用本文: 邓志安, 刘丹丹. CO2驱采出液分离器内构件分离特性数值模拟[J]. 油气储运, 2017, 36(6): 722-727. DOI: 10.6047/j.issn.1000-8241.2017.06.017
DENG Zhian, LIU Dandan. Numerical simulation on separation characteristics of internal components of separator used for CO2 flooding produced fluid[J]. Oil & Gas Storage and Transportation, 2017, 36(6): 722-727. DOI: 10.6047/j.issn.1000-8241.2017.06.017
Citation: DENG Zhian, LIU Dandan. Numerical simulation on separation characteristics of internal components of separator used for CO2 flooding produced fluid[J]. Oil & Gas Storage and Transportation, 2017, 36(6): 722-727. DOI: 10.6047/j.issn.1000-8241.2017.06.017

CO2驱采出液分离器内构件分离特性数值模拟

Numerical simulation on separation characteristics of internal components of separator used for CO2 flooding produced fluid

  • 摘要: CO2驱采出液中含有大量CO2气体,在气液分离过程中易产生泡沫,通过对卧式分离器内部导流板和消泡板的分离特性进行数值模拟,探讨其内部构件对CO2驱采出液分离效果的影响。拟合分离器运行工况下采出液的物性参数,采用CFD中的多相流混合模型,对分离器中导流板的4种放置角度(15°、30°、45°、60°)进行数值模拟,结果表明:导流板放置角度越大,对气液分离的影响越有利,但影响逐渐减弱,在综合考虑导流板使用稳定性及寿命的情况下,选取导流板最优放置角度为45°;采用群体平衡模型(Population Balance Model,PBM)与CFD多相流模型相互耦合,对分离器中放置的1~3个消泡板进行数值模拟,结果表明:分离器内消泡板数量越多,其消泡效率越强,该研究结果为设计更高效CO2驱采出液的分离器提供了一定依据。

     

    Abstract: There is a large amount of CO2 in the produced fluid from CO2 flooding, and a lot of foam is formed in the process of gas and liquid separation. In this paper, the effects of internal components of separators on the separation characteristics of CO2 flooding produced fluid were discussed by performing numerical simulation on the separation characteristics of internal flow deflector and defoaming plate of horizontal separators. The physical property parameters of produced fluid in the operating condition of separator were fitted, and the flow deflector inside the separator was numerically simulated in the conditions of four laying angles (15°, 30°, 45°and 60°) by using the multiphase-flow mixture model in CFD. It is indicated that the larger the laying angle of flow deflector is, the more favorable it is for gas and liquid separation, but the effect diminishes gradually. When the utilization stability and service life of flow deflector is taken into consideration comprehensively, the optimal laying angle of flow deflector is 45°. Finally, separators equipped with 1-3 defoaming plates were numerically simulated by using the mutual coupling between Population Balance Model (PBM) and CFD multiphase flow model. It is shown that defoaming efficiency increases as the number of defoaming plates inside the separator increases. The research results provide the basis for the design of high-efficiency separators used for CO2 flooding produced fluid.

     

/

返回文章
返回