Carbon dioxide capture using a CO2-selective facilitated transport membrane

被引:180
作者
Huang, Jin [1 ]
Zou, Jian [1 ]
Ho, W. S. Winston [1 ]
机构
[1] Ohio State Univ, Dept Mat Sci & Engn, Dept Chem & Biomol Engn, Columbus, OH 43210 USA
关键词
D O I
10.1021/ie070794r
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A novel CO2-selective membrane with the facilitated transport mechanism has been synthesized to capture CO2 from the industrial gas mixtures, including flue gas. Both mobile and fixed amine carriers were incorporated into the cross-linked poly(vinyl alcohol) (PVA) during the membrane synthesis. The membrane showed desirable CO2 permeability (with a suitable effective thickness) and CO2/N-2 selectivity up to 170 degrees C. In the CO2 capture experiments from a gas Mixture with N-2 and H-2, a permeate CO2 dry concentration of >98% was obtained, using steam as the sweep gas. The effects of the feed flow rate and the sweep:feed molar ratio on the membrane separation performance were investigated. A one-dimensional isothermal model was established to examine the performance of a hollow-fiber membrane module composed of the described CO2-selective membrane. The modeling results Show that a CO2 recovery of >95% and a permeate CO2 dry concentration of >98% are achievable from a 1000 standard cubic feet per minute (SCFM) (or 21.06 mol/s) flue gas stream with a 2 ft (0.61 m) hollow-fiber module that contained 980 000 fibers.
引用
收藏
页码:1261 / 1267
页数:7
相关论文
共 36 条
[1]   Separation of CO2 from flue gas:: A review [J].
Aaron, D ;
Tsouris, C .
SEPARATION SCIENCE AND TECHNOLOGY, 2005, 40 (1-3) :321-348
[2]   Facilitated transport of CO2 through immobilized liquid membrane [J].
Al Marzouqi, MH ;
Abdulkarim, MA ;
Marzouk, SA ;
El-Naas, MH ;
Hasanain, HM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (24) :9273-9278
[3]  
Bounaceur R, 2006, ENERGY, V31, P2556, DOI 10.1016/j.energy.2005.10.038
[4]   High-temperature membranes in power generation with CO2 capture [J].
Bredesen, R ;
Jordal, K ;
Bolland, O .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (09) :1129-1158
[5]   KINETICS OF CARBAMATE FORMATION AND BREAKDOWN [J].
CAPLOW, M .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1968, 90 (24) :6795-&
[6]   ON THE LIMITS OF FACILITATED DIFFUSION [J].
CUSSLER, EL ;
ARIS, R ;
BHOWN, A .
JOURNAL OF MEMBRANE SCIENCE, 1989, 43 (2-3) :149-164
[7]   PROTEIN EXTRACTIONS WITH HOLLOW FIBERS [J].
DAHURON, L ;
CUSSLER, EL .
AICHE JOURNAL, 1988, 34 (01) :130-136
[8]   REACTION OF CO2 WITH ETHANOLAMINES [J].
DANCKWERTS, PV .
CHEMICAL ENGINEERING SCIENCE, 1979, 34 (04) :443-446
[9]   Permeation properties to CO2 and N2 of poly(ethylene oxide)-containing and crosslinked polymer films [J].
Hirayama, Y ;
Kase, Y ;
Tanihara, R ;
Sumiyama, Y ;
Kusuki, Y ;
Haraya, K .
JOURNAL OF MEMBRANE SCIENCE, 1999, 160 (01) :87-99
[10]   Modeling of CO2-selective water gas shift membrane reactor for fuel cell [J].
Huang, J ;
El-Azzami, L ;
Ho, WSW .
JOURNAL OF MEMBRANE SCIENCE, 2005, 261 (1-2) :67-75