A novel centrifugal gas liquid pipe separator for high velocity wet gas separation

被引:31
|
作者
Wei, Pengkai [1 ]
Wang, Dong [1 ]
Niu, Pengman [1 ]
Pang, Chenkang [1 ]
Liu, Ming [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
Gas-liquid two-phase flow; Separation; High velocity wet gas; Annular flow; PHASE-ISOLATION; PERFORMANCE;
D O I
10.1016/j.ijmultiphaseflow.2019.103190
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Cyclones are the most widely used separators at present, but it's still difficult to reduce their size to serve as pipe separators. A new type of gas liquid pipe separator for high velocity wet gas is proposed in this paper. The separator is actually a short section of pipe, with a centrifugal device in the center portion and 3 narrow tangential conduits (NTC) in the pipe wall. As gas liquid mixture flows through the centrifugal device downwardly, a strong rotation flow is created. Liquid in the mixture is pushed to the pipe wall by centrifugal force and forms a uniform liquid film with high tangential velocity. Then nearly all the liquid film can directly enter the NTC and be discharged from the pipe relying on its own kinetic energy and inertial, because of the little resistance characteristic of NTC to the liquid film, therefore the whole separation process can be completed within the pipe. The swirl characteristics in the pipe were studied by numerical method, and the simulation results indicated that the swirling liquid film is fairly uniform and the suitable installation position for NTC is about 2.5 pipe diameters downstream of the centrifugal device. A separation model for the pipe separator was established and experiments were carried out to verify the proposed model. The superficial velocity ranges of gas and liquid were 22-72 m/s and 0.07-0.54 m/s, respectively. The experimental results showed that the separation efficiency always increases with the increase of both gas and liquid superficial velocity, generally it is over 0.81, and the maximum attainable is 0.97. However, the separation efficiency will begin to drop if liquid superficial velocity exceeds the critical value U-CSL, due to the onset of unstable liquid film waves. Experimental results also showed that U-CSL, increases with the increase of gas velocity. (C) 2019 Elsevier Ltd. All rights reserved.
引用
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页数:17
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