Mathematical modeling and simulation of carbon dioxide stripping from water using hollow fiber membrane contactors

被引:12
作者
Mehdipourghazi, Mohsen [1 ]
Barati, Sara [1 ]
Varaminian, Farshad [1 ]
机构
[1] Semnan Univ, Fac Chem Petr & Gas Engn, Semnan 3513119111, Iran
关键词
Mathematical modeling; Hollow fiber membrane; Carbon dioxide stripping; Wilke-Chang equation; POLYVINYLIDENE FLUORIDE; CO2; ABSORPTION; EXTRACTION;
D O I
10.1016/j.cep.2015.06.006
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In the present investigation, removal of carbon dioxide from water was examined theoretically using a hollow fiber membrane contactor. A 2D mathematical model with axial and radial diffusions in the membrane contactor was developed. The finite element method was used to solve the governing equations. The results of modeling were in good agreement on the wide range of liquid velocity and temperature with experimental data. The results indicated that, as liquid phase velocity and carbon dioxide concentration in liquid phase increased, the carbon dioxide stripping increased significantly. Also by the increment of the liquid temperature, carbon dioxide stripping flux increased because of carbon dioxide solubility decrement. By increasing gas velocity from 0.02 to 0.07, CO2 stripping flux increases by 7.5%. The diffusion coefficient was computed through the equations of Versteeg and Wilke-Chang. The results revealed that since concentration does not change through the tube and diffusion coefficient is a function of concentration in liquids, the Wilke-Chang equation could better predict the diffusion coefficient than the Versteeg equation. The maximum error in this regard was 6% with solution time of 20 second. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:159 / 164
页数:6
相关论文
共 24 条
[1]   Application of hollow fiber membrane contactor for the removal of carbon dioxide from water under liquid-liquid extraction mode [J].
Agrahari, Gunjan K. ;
Verma, Nishith ;
Bhattacharya, Prashant K. .
JOURNAL OF MEMBRANE SCIENCE, 2011, 375 (1-2) :323-333
[2]   Modeling of chemical absorption of CO2 in membrane contactors [J].
Al-Marzouqi, M. ;
El-Naas, M. ;
Marzouk, S. ;
Abdullatiff, N. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 62 (03) :499-506
[3]   Modeling of CO2 absorption in membrane contactors [J].
Al-Marzouqi, Mohamed H. ;
El-Naas, Muftah H. ;
Marzouk, Sayed A. M. ;
Al-Zarooni, Mohamed A. ;
Abdullatif, Nadia ;
Faiz, Rami .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 59 (03) :286-293
[4]   Carbon Dioxide Capture from Flue Gases Using a Cross-Flow Membrane Contactor and the Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate [J].
Albo, Jonathan ;
Luis, Patricia ;
Irabien, Angel .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (21) :11045-11051
[5]   Effect of membrane structure on mass-transfer in the membrane gas-liquid contacting process using microporous PVDF hollow fibers [J].
Atchariyawut, Supakorn ;
Feng, Chunsheng ;
Wang, Rong ;
Jiraratananon, Ratana ;
Liang, D. T. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :272-281
[6]  
Bird R B., 2002, Transportphenomena
[7]   Using polypropylene and polytetrafluoroethylene membranes in a membrane contactor for CO2 absorption [J].
deMontigny, David ;
Tontiwachwuthikul, Paitoon ;
Chakma, Amit .
JOURNAL OF MEMBRANE SCIENCE, 2006, 277 (1-2) :99-107
[8]   Hollow fiber membrane contactors [J].
Gabelman, A ;
Hwang, ST .
JOURNAL OF MEMBRANE SCIENCE, 1999, 159 (1-2) :61-106
[9]   Mathematical modeling and simulation of CO2 stripping from monoethanolamine solution using nano porous membrane contactors [J].
Ghadiri, Mehdi ;
Marjani, Azam ;
Shirazian, Saeed .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2013, 13 :1-8
[10]   VISCOUS FLOW RELATIVE TO ARRAYS OF CYLINDERS [J].
HAPPEL, J .
AICHE JOURNAL, 1959, 5 (02) :174-177