Numerical investigation on the flow characteristics of liquid oxygen and water in the structured packing

被引:14
作者
Gu, Chenjie [1 ]
Zhang, Ruiping [1 ]
Zhi, Xiaoqin [1 ]
Zhu, Shaolong [1 ]
Qiu, Limin [1 ]
机构
[1] Zhejiang Univ, Inst Refrigerat & Cryogen, Hangzhou 310027, Peoples R China
关键词
Cryogenic distillation; Structured packing; CFD simulation; Hydrodynamic parameters; Liquid oxygen; MASS-TRANSFER; HOLD-UP; PRESSURE-DROP; DISTILLATION-COLUMNS; COMPREHENSIVE MODEL; CFD SIMULATION; GAS-LIQUID; WIRE GAUZE; AREA; EFFICIENCY;
D O I
10.1016/j.cryogenics.2020.103140
中图分类号
O414.1 [热力学];
学科分类号
摘要
The distillation efficiency of the cryogenic air separation unit is significantly affected by the inside flow performance of the cryogenic oxygen and nitrogen mixture in the structured packing. Owing to the difficulties in cryogenic experiments, the development of structured packings in cryogenic distillation often relies on the hydraulic experiments at room temperatures, while the real flow characteristics of the cryogenic fluids in the structured packing are hardly known. In this work, with the help of CFD simulation, a 3-D model combining VOF method was built to study the flow characteristics of liquid oxygen (LOX) in the structured packing, and comparisons with water were also carried out. Effects of liquid load and equivalent contact angle on the flow patterns, the liquid hold-up, the interfacial area and the average film thickness were analyzed. Results show that the flow of water is mainly rivulets, while LOX can form film flow on the packing surface in a large fluid load range due to its small contact angle and surface tension. Because the interfacial area of LOX isn't strongly affected by liquid load, its liquid film thickness could be the main consideration for heat transfer, mass transfer and load selection. Since the variation of contact angle has slight effect on the flow parameters of LOX, the optimization of structured packings for cryogenic distillation may not be expected by the surface micro texture improvements.
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页数:10
相关论文
共 40 条
[1]   Tomographic measurement of liquid hold up and effective interfacial area distributions in a column packed with high performance structured packings [J].
Aferka, S. ;
Viva, A. ;
Brunazzi, E. ;
Marchot, P. ;
Crine, M. ;
Toye, D. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (14) :3413-3422
[2]   Experimental and numerical study of mass transfer efficiency in new wire gauze with high capacity structured packing [J].
Amini, Younes ;
Karimi-Sabet, Javad ;
Esfahany, Mohsen Nasr ;
Haghshenasfard, Masoud ;
Dastbaz, Abolfazl .
SEPARATION SCIENCE AND TECHNOLOGY, 2019, 54 (16) :2706-2717
[3]   CFD simulation of the structured packings: A review [J].
Amini, Younes ;
Esfahany, Mohsen Nasr .
SEPARATION SCIENCE AND TECHNOLOGY, 2019, 54 (15) :2536-2554
[4]   Experimental and numerical study of multiphase flow in new wire gauze with high capacity structured packing [J].
Amini, Younes ;
Karimi-Sabet, Javad ;
Esfahany, Mohsen Nasr .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2016, 108 :35-43
[5]   Experimental and Numerical Simulation of Dry Pressure Drop in High-Capacity Structured Packings [J].
Amini, Younes ;
Karimi-Sabet, Javad ;
Esfahany, Mohsen Nasr .
CHEMICAL ENGINEERING & TECHNOLOGY, 2016, 39 (06) :1161-1170
[6]  
Basden MA, 2014, CHARACTERIZATION STR
[7]   Liquid Holdup Profiles in Structured Packing Determined via Neutron Radiography [J].
Basden, Michael ;
Eldridge, R. Bruce ;
Farone, John ;
Feng, Esther ;
Hussey, Daniel S. ;
Jacobson, David L. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (48) :17263-17269
[8]  
Bergman TL., 2007, FUNDAMENTALS HEAT MA
[9]  
Billet R., 1993, CHEM ENG TECHNOL, V16, P1, DOI [10.1002/ceat.270160102, DOI 10.1002/CEAT.270160102]
[10]   A CONTINUUM METHOD FOR MODELING SURFACE-TENSION [J].
BRACKBILL, JU ;
KOTHE, DB ;
ZEMACH, C .
JOURNAL OF COMPUTATIONAL PHYSICS, 1992, 100 (02) :335-354