Three-dimensional Computational Fluid Dynamics Modeling of Two-phase Flow in a Structured Packing Column

被引:15
作者
Zhang Xiaobin [1 ]
Yao Lei [1 ]
Qiu Limin [1 ]
Zhang Xuejun [1 ]
机构
[1] Zhejiang Univ, Inst Refrigerat & Cryogen, Hanghzou 310027, Peoples R China
基金
中国国家自然科学基金;
关键词
structured packing column; two-phase flow; computational fluid dynamics; three-dimension; GAS-LIQUID FLOW; DISTILLATION-COLUMNS; PRESSURE-DROP; MASS-TRANSFER; COMPREHENSIVE MODEL; CFD SIMULATION; PERFORMANCE;
D O I
10.1016/S1004-9541(13)60576-5
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Characterizing the complex two-phase hydrodynamics in structured packed columns requires a powerful modeling tool. The traditional two-dimensional model exhibits limitations when one attempts to model the detailed two-phase flow inside the columns. The present paper presents a three-dimensional computational fluid dynamics (CFD) model to simulate the two-phase flow in a representative unit of the column. The unit consists of an entire corrugation channel and describes well the real liquid flow conditions. The detailed unsteady two-phase 3D CFD calculations on column packed with Flexipak 1Y were implemented within the volume of fluid (VOF) mathematical framework. The CFD model was validated by comparing the calculated thickness of liquid film with the available experimental data. Special attention was given to quantitative analysis of the effects of gravity on the hydrodynamics. Fluctuations in the liquid mass flow rate and the calculated pressure drop loss were found to be qualitatively in agreement with the experimental observations.
引用
收藏
页码:959 / 966
页数:8
相关论文
共 20 条
[1]  
Baten J.M.V, 2002, CHEM ENG SCI, V57, P1531
[2]  
BATEN JM, 2001, CATAL TODAY, V69, P371
[3]  
Beata S, 2003, CHEM ENG TECHNOL, V26, P580
[4]   Laminar film flow down a wavy incline [J].
Bontozoglou, V ;
Papapolymerou, G .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1997, 23 (01) :69-79
[5]   CFD Simulation of Flow and Mass Transfer in Structured Packing Distillation Columns [J].
Chen Jiangbo ;
Liu Chunjiang ;
Yuan Xigang ;
Yu Guocong .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2009, 17 (03) :381-388
[6]   CFD simulation of mass transfer efficiency and pressure drop in a structured packed distillation column [J].
Fard, M. Haghshenas ;
Zivdar, M. ;
Rahimi, R. ;
Esfahany, M. Nasr ;
Afacan, A. ;
Nandakumar, K. ;
Chuang, K. T. .
CHEMICAL ENGINEERING & TECHNOLOGY, 2007, 30 (07) :854-861
[7]  
Fluent, 2006, FLUENT HELP DOC
[8]   Design method for distillation columns filled with metallic, ceramic, or plastic structured packings [J].
Gualito, JJ ;
Cerino, FJ ;
Cardenas, JC ;
Rocha, JA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (05) :1747-1757
[9]   Counter-current gas-liquid flow and incipient flooding in inclined small diameter tubes [J].
Pantzali, M. N. ;
Mouza, A. A. ;
Paras, S. V. .
CHEMICAL ENGINEERING SCIENCE, 2008, 63 (15) :3966-3978
[10]   Pressure drop through structured packings: Breakdown into the contributing mechanisms by CFD modeling [J].
Petre, CF ;
Larachi, F ;
Iliuta, I ;
Grandjean, BPA .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (01) :163-177