Analysis of hybrid membrane and chemical absorption systems for CO2 capture

被引:10
作者
Binns, Michael [1 ]
Oh, Se-Young [1 ]
Kwak, Dong-Hun [1 ]
Kim, Jin-Kuk [1 ]
机构
[1] Hanyang Univ, Dept Chem Engn, Seoul 133791, South Korea
关键词
Membrane Separation; Chemical Absorption; CO2; Capture; Process Design; Hybrid Separation; HOLLOW-FIBER MEMBRANE; POWER-PLANT; GAS SEPARATION; MONOETHANOLAMINE; SIMULATION; MODEL;
D O I
10.1007/s11814-014-0188-y
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Amine-based absorption of CO2 is currently the industry standard technology for capturing CO2 emitted from power plants, refineries and other large chemical plants. However, more recently there have been a number of competing technologies under consideration, including the use of membranes for CO2 separation and purification. We constructed and analyzed two different hybrid configurations combining and connecting chemical absorption with membrane separation. For a particular flue gas which is currently treated with amine-based chemical absorption at a pilot plant we considered and tested how membranes could be integrated to improve the performance of the CO2 capture. In particular we looked at the CO2 removal efficiency and the energy requirements. Sensitivity analysis was performed varying the size of the membranes and the solvent flow rate.
引用
收藏
页码:383 / 389
页数:7
相关论文
共 18 条
[1]   Hybrid membrane cryogenic process for post-combustion CO2 capture [J].
Belaissaoui, Bouchra ;
Le Moullec, Yann ;
Willson, David ;
Favre, Eric .
JOURNAL OF MEMBRANE SCIENCE, 2012, 415 :424-434
[2]   Hybrid processes for the removal of acid gases from natural gas [J].
Bhide, BD ;
Voskericyan, A ;
Stern, SA .
JOURNAL OF MEMBRANE SCIENCE, 1998, 140 (01) :27-49
[3]  
BRAVO JL, 1985, HYDROCARB PROCESS, V64, P91
[4]   Simulation and optimization for power plant flue gas CO2 absorption-stripping systems [J].
Chang, H ;
Shih, CM .
SEPARATION SCIENCE AND TECHNOLOGY, 2005, 40 (04) :877-909
[5]   Modeling multicomponent gas separation using hollow-fiber membrane contactors [J].
Coker, DT ;
Freeman, BD ;
Fleming, GK .
AICHE JOURNAL, 1998, 44 (06) :1289-1302
[6]   Modeling of CO2 capture by aqueous monoethanolamine [J].
Freguia, S ;
Rochelle, GT .
AICHE JOURNAL, 2003, 49 (07) :1676-1686
[7]   Dynamic simulation of multicomponent gas separation by hollow-fiber membrane module: Nonideal mixing flows in permeate and residue sides using the tanks-in-series model [J].
Katoh, Takashi ;
Tokumura, Masahiro ;
Yoshikawa, Hidemi ;
Kawase, Yoshinori .
SEPARATION AND PURIFICATION TECHNOLOGY, 2011, 76 (03) :362-372
[8]   A study on the carbon dioxide recovery from 2 ton-CO2/day pilot plant at LNG based power plant [J].
Lee, Seungmoon ;
Maken, Sanjeev ;
Park, Jin-Won ;
Song, Ho-Jun ;
Park, Jong Jin ;
Shim, Jae-Goo ;
Kim, Jun-Han ;
Eum, Hee-Moon .
FUEL, 2008, 87 (8-9) :1734-1739
[9]   Power plant post-combustion carbon dioxide capture: An opportunity for membranes [J].
Merkel, Tim C. ;
Lin, Haiqing ;
Wei, Xiaotong ;
Baker, Richard .
JOURNAL OF MEMBRANE SCIENCE, 2010, 359 (1-2) :126-139
[10]   Post-combustion CO2 capture process: Equilibrium stage mathematical model of the chemical absorption of CO2 into monoethanolamine (MEA) aqueous solution [J].
Mores, Patricia ;
Scenna, Nicolas ;
Mussati, Sergio .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2011, 89 (09) :1587-1599