Selection and characterization of phase-change solvent for carbon dioxide capture: precipitating system

被引:25
作者
Ma'mun, Sholeh [1 ]
Kim, Inna [1 ]
机构
[1] SINTEF Mat & Chem, N-7465 Trondheim, Norway
来源
GHGT-11 | 2013年 / 37卷
关键词
carbon dioxide capture; absorption; equilibrium; amino acid salt; precipitating system; CO2; CAPTURE; 30-MASS-PERCENT MONOETHANOLAMINE; PILOT-PLANT; SOLUBILITY; ABSORPTION; MEA; METHYLDIETHANOLAMINE; TECHNOLOGY;
D O I
10.1016/j.egypro.2013.05.119
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
Characterization of a precipitating solvent for CO2 capture was performed. Aqueous solution of 5m' potassium salt of sarcosine (KSar) that was precipitated at CO2 loading of 0.52 was selected. The equilibrium solubility of CO2 in the solution was measured over a range of temperatures from 40 to 120 degrees C. The SOFT model was implemented to predict the vapor-liquid-solid equilibrium (VLSE) data for the CO2-KSar-H2O system. The vapor pressures of the solution were measured at temperatures between 53 and 130 degrees C. The heat of absorption was also measured at 40 degrees C. In addition, the heat of absorption of CO2 in the solution was estimated from the VLSE data by use of the Gibbs-Helmholtz equation and was able to predict well the precipitation occurred in the system. (C) 2013 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:331 / 339
页数:9
相关论文
共 21 条
[1]  
Alstom, 401021507 DOENETL
[2]  
Aronu UE, 2012, GHGT 11 KYOT J UNPUB
[3]   Solubility of CO2 in 15, 30, 45 and 60 mass% MEA from 40 to 120 °C and model representation using the extended UNIQUAC framework [J].
Aronu, Ugochukwu E. ;
Gondal, Shahla ;
Hessen, Erik T. ;
Haug-Warberg, Tore ;
Hartono, Ardi ;
Hoff, Karl A. ;
Svendsen, Hallvard F. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (24) :6393-6406
[4]   Studies on absorption and regeneration for CO2 capture by aqueous ammonia [J].
Chen, Haisheng ;
Dou, Binlin ;
Song, Yongchen ;
Xu, Yujie ;
Wang, Xueju ;
Zhang, Yi ;
Du, Xu ;
Wang, Chao ;
Zhang, Xuehui ;
Tan, Chunqin .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2012, 6 :171-178
[5]   Carbon dioxide absorption with aqueous potassium carbonate promoted by piperazine [J].
Cullinane, JT ;
Rochelle, GT .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (17) :3619-3630
[6]   CO2 capture in small size cogeneration plants:: Technical and economical considerations [J].
Desideri, U ;
Corbelli, R .
ENERGY CONVERSION AND MANAGEMENT, 1998, 39 (09) :857-867
[7]  
Feron PHM, 2004, GHGT 7 VANC CAN
[8]   Pilot plant studies of the CO2 capture performance of aqueous MEA and mixed MEA/MDEA solvents at the University of Regina CO2 capture technology development plant and the Boundary Dam CO2 capture demonstration [J].
Idem, R ;
Wilson, M ;
Tontiwachwuthikul, P ;
Chakma, A ;
Veawab, A ;
Aroonwilas, A ;
Gelowitz, D .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (08) :2414-2420
[9]   Towards Commercial Application of a Second-Generation Post-Combustion Capture Technology - Pilot Plant Validation of the Siemens Capture Process and Implementation of a First Demonstration Case [J].
Jockenhoevel, Tobias ;
Schneider, Ruediger .
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 :1451-1458
[10]   THE SOLUBILITY OF CO2 IN A 30-MASS-PERCENT MONOETHANOLAMINE SOLUTION [J].
JOU, FY ;
MATHER, AE ;
OTTO, FD .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1995, 73 (01) :140-147