Investigation on separation characteristics of gas-liquid two-phase flow around the perforated tube

被引:4
作者
Wang, Jinzhi [1 ]
Wang, Yechun [1 ,2 ]
Xie, Xiangdong [1 ]
Xu, Qiang [1 ,2 ]
Wang, Jiang [1 ]
Guo, Liejin [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
[2] Xinjin Weihua Inst Clean Energy Res, Foshan 528216, Peoples R China
基金
中国国家自然科学基金;
关键词
Flow around the perforated tube; Gas-liquid two-phase flow; Wake region; Separation characteristics; CROSS-FLOW; PRESSURE-DROP; HEAT-TRANSFER; IN-LINE; FRACTION; PATTERN; BUBBLE; MODEL; HYDRODYNAMICS; SIMULATION;
D O I
10.1016/j.nucengdes.2023.112200
中图分类号
TL [原子能技术]; O571 [原子核物理学];
学科分类号
0827 ; 082701 ;
摘要
Gas-liquid separator plays an important role in the reactor fission gas removal system. Utilizing the differential pressure formed by flow around the perforated tube, the separator achieves gas-liquid separation, meanwhile having advantages such as simple structure. The evolution characteristics of gas-liquid interface and the vari-ation of parameters such as separation efficiency and pressure drop under plug flow and slug flow are investi-gated. The void fraction in wake region is only related to the inlet volumetric fraction. The variation of air separation efficiency with inlet volumetric fraction is influenced by the inlet flow pattern, and the separation purity increases with the inlet volumetric fraction. The prediction methods of air separation efficiency, pressure drop and other parameters based on Weber number and liquid phase Reynolds number are obtained in accor-dance with dimensional analysis and minimum kinetic energy principle with the prediction accuracy within +/- 20 %, which provides guidance for practical application and optimization.
引用
收藏
页数:13
相关论文
共 51 条
[1]   Flow Pattern and Slug Dynamics Around a Flow Splitter [J].
Alamu, M. B. ;
Azzopardi, B. J. .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2011, 133 (12)
[2]   A metastable wet steam turbine stage model [J].
Bassel, WS ;
Gomes, AV .
NUCLEAR ENGINEERING AND DESIGN, 2002, 216 (1-3) :113-119
[3]  
Delenne B., 1997, ASME INT MECH ENG C, V26768, P349
[4]   Design and optimisation of impedance probes for void fraction measurements [J].
Devia, F ;
Fossa, M .
FLOW MEASUREMENT AND INSTRUMENTATION, 2003, 14 (4-5) :139-149
[5]   Two-dimensional CFD model for the prediction of flow pattern, pressure drop and heat transfer coefficient in bubble column reactors [J].
Dhotre, MT ;
Joshi, JB .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2004, 82 (A6) :689-707
[6]   PITCH-TO-DIAMETER EFFECT ON 2-PHASE FLOW ACROSS AN IN-LINE TUBE BUNDLE [J].
DOWLATI, R ;
KAWAJI, M ;
CHAN, AMC .
AICHE JOURNAL, 1990, 36 (05) :765-772
[7]  
DOWLATI R, 1992, J FLUID ENG-T ASME, V114, P450, DOI 10.1115/1.2910052
[8]   An improved void fraction model for two-phase cross-flow in horizontal tube bundles [J].
Feenstra, PA ;
Weaver, DS ;
Judd, RL .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2000, 26 (11) :1851-1873
[9]   Design and performance of a conductance probe for measuring the liquid fraction in two-phase gas-liquid flows [J].
Fossa, M .
FLOW MEASUREMENT AND INSTRUMENTATION, 1998, 9 (02) :103-109
[10]   Gas-liquid distribution in the developing region of horizontal intermittent flows [J].
Fossa, M .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2001, 123 (01) :71-80