Investigation of CO2 removal by immobilized carbonic anhydrase enzyme in a hollow-fiber membrane bioreactor

被引:41
作者
Iliuta, Ion [1 ]
Iliuta, Maria C. [1 ]
机构
[1] Laval Univ, Dept Chem Engn, Quebec City, PQ G1V 0A6, Canada
关键词
CO2; removal; carbonic anhydrase enzyme; hollow-fiber membrane bioreactor; membrane partial wetting; modeling; MASS-TRANSFER; CAPTURE; HYDRATION; CONTACTORS; ABSORPTION; KINETICS; DIOXIDE; MICROREACTOR; DEGRADATION; SEPARATION;
D O I
10.1002/aic.15646
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gas-liquid membrane contactors are compelling candidate bioreactors for implementing CO2 capture because of large mass transfer rates and liquid-solid interfaces, low pressure drop, low axial dispersion and mixing, modularity, simple scale-up or scale-down, and operational suppleness. Binding the carbonic anhydrase (CA) enzyme on the membrane surface adds extra advantages due to the impressive large hydration turnover number and offers an attractive way for CO2 capture. This novel approach to CO2 removal by immobilized CA in a hollow-fiber membrane bioreactor (HFMB) was investigated via a multiscale steady-state model, under gas-filled and partially liquid-filled membrane pores conditions. The impact of CA loading, buffer acid-base constant and concentration, membrane wetting, uncatalyzed/catalyzed CO2 hydration in the wetted membrane zone, operating conditions, and cocurrent/countercurrent flow orientation on the HFMB performance was analyzed. The results showed that this low-cost, green, and environmentally friendly technology could be an appealing alternative to CO2 capture from stationary emissions sources. (c) 2017 American Institute of Chemical Engineers AIChE J, 63: 2996-3007, 2017
引用
收藏
页码:2996 / 3007
页数:12
相关论文
共 35 条
[1]   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
[2]   Stability of aqueous amine solutions to thermal and oxidative degradation in the absence and the presence of CO2 [J].
Bougie, Francis ;
Iliuta, Maria C. .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2014, 29 :16-21
[3]   Analysis of Laplace-Young equation parameters and their influence on efficient CO2 capture in membrane contactors [J].
Bougie, Francis ;
Iliuta, Maria C. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2013, 118 :806-815
[4]  
Bucholz T. L., 2014, U.S. Patent, Patent No. [8,895,280B2, 8895280]
[5]   Membrane-solvent selection for CO2 removal using membrane gas-liquid contactors [J].
Dindore, VY ;
Brilman, DWF ;
Geuzebroek, FH ;
Versteeg, GF .
SEPARATION AND PURIFICATION TECHNOLOGY, 2004, 40 (02) :133-145
[6]   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
[7]  
Field CB, 2014, CLIMATE CHANGE 2014: IMPACTS, ADAPTATION, AND VULNERABILITY, PT A: GLOBAL AND SECTORAL ASPECTS, P1
[8]   A study of the mass transfer of CO2 through different membrane materials in the membrane gas absorption process [J].
Franco, Julianna ;
Demontigny, David ;
Kentish, Sandra ;
Perera, Jilska ;
Stevens, Geoff .
SEPARATION SCIENCE AND TECHNOLOGY, 2008, 43 (02) :225-244
[9]   Diffusion coefficients and viscosities of CO2+H2O, CO2+CH3OH, NH3+H2O, and NH3+CH3OH liquid mixtures [J].
Frank, MJW ;
Kuipers, JAM ;
vanSwaaij, WPM .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1996, 41 (02) :297-302
[10]  
Froment G.F., 2011, Chemical Reactor Analysis and Design, VThird