Cyclone separator for gas-liquid mixture with high flux density

被引:22
作者
Mikheev, Nikolay [1 ]
Saushin, Ilya [1 ]
Paereliy, Anton [1 ]
Kratirov, Dmitry [2 ]
Levin, Kirill [3 ]
机构
[1] Russian Acad Sci, Fed State Budgetary Inst Sci, Kazan Sci Ctr, 2-31 Lobachevsky St,POB 261, Kazan 420111, Russia
[2] Kazan Natl Res Tech Univ, 10 K Marx St, Kazan 420111, Russia
[3] All Russian Res Inst Flow Metering, Fed State Unitary Enterprise, 7A Vtoraya Azinskaya St, Kazan 420088, Russia
关键词
Cyclone separator; Separation efficiency; High flux density; Upward flowing film; Droplet entrainment; TURBULENT SWIRLING FLOW; NUMERICAL-SIMULATION; DYNAMIC CYCLONE; EFFICIENCY; PERFORMANCE; DESIGN; REENTRAINMENT; OPTIMIZATION; PREDICTIONS; COLLECTION;
D O I
10.1016/j.powtec.2018.08.040
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The study is aimed at improvement of efficiency of a gas-liquid separator operating at the pressure of 2.5 MPa and high flux density in the cyclone body. The submitted schematic construction of the separator provides the reduced dynamic head of gas in the zones with increased liquid phase concentration and prevents the entrainment of separated liquid to the outlet receiver. The receiver consisting of a conical converging channel and an externally finned circular pipe is located in the middle of cylindrical cyclone body. A fin-and-tube flow conditioner is mounted upstream of the converging channel inlet. Detailed flow structure in the separator has been obtained from numerical study based on Reynolds-averaged Navier-Stokes equations with anisotropic Reynolds stress turbulence model. Simulation results were involved in estimation of the main performance characteristics of the separator and probability of droplet entrainment and upwards flowing film. Experimental research on a 1:2 separator model allowed estimation of separation efficiency and flow resistance coefficient of the separator. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:326 / 333
页数:8
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