Modeling of carbon dioxide absorption in a gas/liquid membrane contactor

被引：6

作者：

Alavinasab, Amir ^{[1
]}

Kaghazchi, Tahereh ^{[1
]}

Ravanchi, Maryam Takht ^{[2
]}

Shabani, Keyvan ^{[3
]}

机构：

[1] Amirkabir Univ Technol, Ctr Excellence Petrochem, Dept Chem Engn, Tehran Polytech, Tehran, Iran

[2] Res & Technol Co, Natl Petrochem Co, Tehran, Iran

[3] Engn Res Inst, Tehran, Iran

来源：

DESALINATION AND WATER TREATMENT | 2011年 / 29卷 / 1-3期

关键词：

Flat sheet membrane contactor; Carbon dioxide; Absorption; LIQUID-MEMBRANE; FACILITATED TRANSPORT; AMINE SOLUTIONS; CO2; ABSORPTION; SEPARATION; KINETICS; SINGLE;

D O I：

10.5004/dwt.2011.1204

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In this study, the behavior of CO2 absorption in flat sheet membrane contactors is developed. Physical and chemical absorption of CO2 in co-current and counter-current flow were studied using both distilled water and 2-amino-2 methyl 1-propanol (AMP) as a solvent in the model. The effect of flow pattern, solvent type and gas and liquid velocity on absorption of carbon dioxide through the membrane contactor is obtained. The results indicate that the use of AMP instead of water leads to a better separation for carbon dioxide. Furthermore, unlike the liquid velocity, lower value of gas velocity showed higher performance for absorption.

引用

页码：336 / 342

页数：7

共 19 条

[1] 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

[2] Separation of CO2 from CH4 by using gas-liquid membrane contacting process [J].

Atchariyawut, Supakorn ;

Jiraratananon, Ratana ;

Wang, Rong .

JOURNAL OF MEMBRANE SCIENCE, 2007, 304 (1-2) :163-172

[3] Modeling CO2-facilitated transport across a diethanolamine liquid membrane [J].

Bao, LH ;

Trachtenberg, MC .

CHEMICAL ENGINEERING SCIENCE, 2005, 60 (24) :6868-6875

[4] Facilitated transport of CO2 across a liquid membrane:: Comparing enzyme, amine, and alkaline [J].

Bao, Lihong ;

Trachtenberg, Michael C. .

JOURNAL OF MEMBRANE SCIENCE, 2006, 280 (1-2) :330-334

[5] GAS-LIQUID MASS-TRANSFER WITH PARALLEL REVERSIBLE-REACTIONS .1. ABSORPTION OF CO2 INTO SOLUTIONS OF STERICALLY HINDERED AMINES [J].

BOSCH, H ;

VERSTEEG, GF ;

VANSWAAIJ, WPM .

CHEMICAL ENGINEERING SCIENCE, 1989, 44 (11) :2723-2734

[6] KINETICS OF THE REACTION OF CO2 WITH THE STERICALLY HINDERED AMINE 2-AMINO-2-METHYLPROPANOL AT 298-K [J].

BOSCH, H ;

VERSTEEG, GF ;

VANSWAAIJ, WPM .

CHEMICAL ENGINEERING SCIENCE, 1990, 45 (05) :1167-1173

[7] CO2 removal from a gas stream by membrane contactor [J].

Bottino, Aldo ;

Capannelli, Gustavo ;

Comite, Antonio ;

Di Felice, Renzo ;

Firpo, Raffaella .

SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 59 (01) :85-90

[8]

Cussler E.L., 2009, CAMBRIDGE SERIES CHE, Vthird

[9] CO2/H2 separation by facilitated transport membranes immobilized with aqueous single and mixed amine solutions: Experimental and modeling study [J].

Gorji, Aliakbar Heydari ;

Kaghazchi, Tahereh .

JOURNAL OF MEMBRANE SCIENCE, 2008, 325 (01) :40-49

[10] Analytical approximate solution of competitive facilitated transport of acid gases through liquid membranes [J].

Heydari, Aliakbar ;

Kaghazchi, Tahereh ;

Kargari, Ali .

DESALINATION, 2009, 235 (1-3) :245-263

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