Membrane contactors for intensified post-combustion carbon dioxide capture by gas-liquid absorption processes

被引:73
作者
Favre, E. [1 ]
Svendsen, H. F. [2 ]
机构
[1] Nancy Univ, LRGP CNRS, F-54001 Nancy, France
[2] NTNU, Dept Chem Engn, N-7491 Trondheim, Norway
关键词
Membrane contactors; Post-combustion; CO2; Capture; Packed columns; Intensification; MASS-TRANSFER; MICROPOROUS MEMBRANES; CO2; SEPARATION; REMOVAL; PERFORMANCES; PIPERAZINE; ABSORBENT;
D O I
10.1016/j.memsci.2012.03.019
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
The use of membrane contactors for post-combustion CO2 capture by absorption into a chemical solvent is currently one of the most intensively investigated topics in membrane science. The main (if not the only) target of employing membra:ne contactors for this application is to provide a significant reduction in size of the absorption unit, as compared to the classical gas-liquid absorption technology, based on packed columns. Surprisingly, this key performance characteristic, which is best expressed through a so-called intensification factor, remains essentially unreported in studies dedicated to CO2 absorption in membrane contactors. In this article, we recall the state of the art in terms of operating conditions and process performance for packed columns applied to CO2 capture. Based on this, a series of challenges for membrane material design and critical process engineering issues are discussed in order to set up a methodology for a better comparison between membrane contactors and packed columns. More specifically, an average volumetric CO2 absorption capacity around 1 mol CO2 m(-3) s(-1) is proposed as a baseline performance of packed columns in order to estimate the intensification factor of membrane contactors. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 7
页数:7
相关论文
共 47 条
[1]
Mass transfer studies of high performance structured packing for CO2 separation processes [J].
Aroonwilas, A ;
Tontiwachwuthikul, P .
ENERGY CONVERSION AND MANAGEMENT, 1997, 38 :S75-S80
[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]
Use of nonporous polymeric flat-sheet gas-separation membranes in a membrane-liquid contactor: Experimental studies [J].
Bessarabov, DG ;
Jacobs, EP ;
Sanderson, RD ;
Beckman, IN .
JOURNAL OF MEMBRANE SCIENCE, 1996, 113 (02) :275-284
[4]
Membrane Contactors for Postcombustion Carbon Dioxide Capture: A Comparative Study of Wetting Resistance on Long Time Scales [J].
Chabanon, Elodie ;
Roizard, Denis ;
Favre, Eric .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (13) :8237-8244
[5]
Comparing the absorption performance of packed columns and membrane contactors [J].
deMontigny, D ;
Tontiwachwuthikul, P ;
Chakma, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (15) :5726-5732
[6]
Evaluation of the removal of CO2 using membrane contactors: Membrane wettability [J].
El-Naas, Muftah H. ;
Al-Marzouqi, Mohamed ;
Marzouk, Sayed A. ;
Abdullatif, Nadia .
JOURNAL OF MEMBRANE SCIENCE, 2010, 350 (1-2) :410-416
[8]
Separation of carbon dioxide from offshore gas turbine exhaust [J].
FalkPedersen, O ;
Dannstrom, H .
ENERGY CONVERSION AND MANAGEMENT, 1997, 38 :S81-S86
[9]
FalkPederson O., 2001, US Patent, Patent No. [6 228 145, 6228145]
[10]
CO2 separation with polyolefin membrane contactors and dedicated absorption liquids:: performances and prospects [J].
Feron, PHM ;
Jansen, AE .
SEPARATION AND PURIFICATION TECHNOLOGY, 2002, 27 (03) :231-242