Membrane pilot plant trials of CO2 separation from flue gas

被引：37

作者：

Scholes, Colin A. ^{[1
]}

Qader, Abdul ^{[2
]}

Stevens, Geoff W. ^{[3
]}

Kentish, Sandra E. ^{[1
]}

机构：

[1] Univ Melbourne, Dept Chem & Biomol Engn, Melbourne, Vic 3010, Australia

[2] Univ Melbourne, Melbourne, Vic 3010, Australia

[3] Univ Melbourne, Dept Chem & Biomol Engn, Chem Engn, Melbourne, Vic 3010, Australia

来源：

GREENHOUSE GASES-SCIENCE AND TECHNOLOGY | 2015年 / 5卷 / 03期

关键词：

membrane; carbon dioxide; flue gas; pilot plant; facilitated transport; CARBON-DIOXIDE CAPTURE; SPIRAL WOUND MODULES; WATER-VAPOR; FACILITATED TRANSPORT; POLYMERIC MEMBRANES; POLYIMIDE MEMBRANES; MASS-TRANSFER; FLOW; PERMEATION; CHANNELS;

D O I：

10.1002/ghg.1498

中图分类号：

TE [石油、天然气工业]; TK [能源与动力工程];

学科分类号：

0807 ; 0820 ;

摘要：

Industrial trials of membrane separation of CO2 from flue gas generated by a lignite-fired power station are reported. A hollow fiber Air Products PRISM and a spiral wound Dow Filmtec (R) NF3838/30FF membrane were separately trialed. The CO2 permeance and selectivity through the PRISM membrane fell significantly in the initial hours of operation, reflecting competitive sorption effects and concentration polarisation. Alternatively, the wet flue gas enabled a facilitated transport mechanism to operate for the NF3838/30FF membrane and the CO2 permeance and selectivity increased significantly compared to the dry membrane. Standard correlations were able to simulate the pressure drops through the modules.(c) 2015 Society of Chemical Industry and John Wiley & Sons, Ltd

引用

页码：229 / 237

页数：9

共 31 条

[1]

[Anonymous], 2007, PRISM PA1020 NITR ME

[2]

Baker RW, 2008, ADV MEMBRANE TECHNOL

[3] Modeling of the sorption and transport properties of water vapor in polyimide membranes [J].

Chen, George Q. ;

Scholes, Colin A. ;

Doherty, Cara M. ;

Hill, Anita J. ;

Qiao, Greg G. ;

Kentish, Sandra E. .

JOURNAL OF MEMBRANE SCIENCE, 2012, 409 :96-104

[4] SPACER CHARACTERIZATION AND PRESSURE-DROP MODELING IN SPACER-FILLED CHANNELS FOR ULTRAFILTRATION [J].

DACOSTA, AR ;

FANE, AG ;

WILEY, DE .

JOURNAL OF MEMBRANE SCIENCE, 1994, 87 (1-2) :79-98

[5] Performance modelling of a carbon dioxide removal system for power plants [J].

Desideri, U ;

Paolucci, A .

ENERGY CONVERSION AND MANAGEMENT, 1999, 40 (18) :1899-1915

[6] Flow management in nanofiltration spiral wound modules with ladder-type spacers [J].

Geraldes, V ;

Semiao, V ;

de Pinho, MN .

JOURNAL OF MEMBRANE SCIENCE, 2002, 203 (1-2) :87-102

[7] CO2 capture by sub-ambient membrane operation [J].

Hasse, David ;

Kulkarni, Sudhir ;

Sanders, Ed ;

Corson, E. ;

Tranier, Jean-Pierre .

GHGT-11, 2013, 37 :993-1003

[8] Reducing the cost of CO2 capture from flue gases using membrane technology [J].

Ho, Minh T. ;

Allinson, Guy W. ;

Wiley, Dianne E. .

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (05) :1562-1568

[9] Cake-enhanced concentration polarization: A new fouling mechanism for salt-rejecting membranes [J].

Hoek, EMV ;

Elimelech, M .

ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2003, 37 (24) :5581-5588

[10]

Koros W., 1991, Membrane Separation Systems -Recent Developments and Future Directions

← 1 2 3 4 →