Equilibrium solubility of carbon dioxide in 2(methylamino)ethanol

被引:24
作者
Haider, Hawar A. M. [1 ]
Yusoff, Rozita [1 ]
Aroua, M. K. [1 ]
机构
[1] Univ Malaya, Dept Chem Engn, Fac Engn, Kuala Lumpur 50603, Malaysia
关键词
Absorption; Alkanolamine; 2(Methylamino)ethanol; CO(2) solubility; Equilibrium constants; VAPOR-LIQUID-EQUILIBRIA; AQUEOUS-SOLUTIONS; HYDROGEN-SULFIDE; MODEL; CO2; SYSTEMS; ALKANOLAMINES; PREDICTION; MDEA; DEA;
D O I
10.1016/j.fluid.2011.01.016
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this paper the equilibrium solubility of carbon dioxide in 1.0 M. 2.0 M and 4.0 M 2(methylamino)ethanol (MAE) is measured at 303, 313 and 333 K. and at CO(2) partial pressures ranging from 1 to 100 kPa using stirred cell reactor. The Kent-Eisenberg model was used to predict the solubility of carbon dioxide in MAE solutions. The equilibrium constant representing hydrolysis of carbamate ion is correlated with temperature, CO(2) partial pressure and amine concentration by non-linear regression, using experimental results of carbamate ion concentrations. The model predicted results showed good agreement with the experimental solubility results. The solubility profile of CO(2) in MAE showed better performance when compared with other commercial amines. (c) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:162 / 167
页数:6
相关论文
共 24 条
[1]   Effect of piperazine on CO2 loading in aqueous solutions of MDEA at low pressure [J].
Ali, BS ;
Aroua, MK .
INTERNATIONAL JOURNAL OF THERMOPHYSICS, 2004, 25 (06) :1863-1870
[2]  
ALI BS, 2007, THESIS U MALAYA MALA
[3]   MODEL OF VAPOR LIQUID EQUILIBRIA FOR AQUEOUS ACID GAS ALKANOLAMINE SYSTEMS USING THE ELECTROLYTE NRTL EQUATION [J].
AUSTGEN, DM ;
ROCHELLE, GT ;
PENG, X ;
CHEN, CC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (07) :1060-1073
[4]   Prediction of equilibrium solubility of carbon dioxide in aqueous 2-amino-2-methyl-13-propanediol solutions [J].
Baek, JI ;
Yoon, JH ;
Eum, HM .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2000, 17 (04) :484-487
[5]   Modeling of CO2 solubility and carbamate concentration in DEA, MDEA and their mixtures using the Deshmukh-Mather model [J].
Benamor, A ;
Aroua, MK .
FLUID PHASE EQUILIBRIA, 2005, 231 (02) :150-162
[6]   DEGRADATION OF AQUEOUS DEA SOLUTIONS IN A HEAT-TRANSFER TUBE [J].
CHAKMA, A ;
MEISEN, A .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1987, 65 (02) :264-273
[7]  
CHAKRAVARTY T, 1985, THESIS CLARKSON U PO
[8]   A LOCAL COMPOSITION MODEL FOR THE EXCESS GIBBS ENERGY OF AQUEOUS-ELECTROLYTE SYSTEMS [J].
CHEN, CC ;
EVANS, LB .
AICHE JOURNAL, 1986, 32 (03) :444-454
[9]   A MATHEMATICAL-MODEL FOR EQUILIBRIUM SOLUBILITY OF HYDROGEN-SULFIDE AND CARBON-DIOXIDE IN AQUEOUS ALKANOLAMINE SOLUTIONS [J].
DESHMUKH, RD ;
MATHER, AE .
CHEMICAL ENGINEERING SCIENCE, 1981, 36 (02) :355-362
[10]   VAPOR-LIQUID-EQUILIBRIA IN MULTICOMPONENT AQUEOUS-SOLUTIONS OF VOLATILE WEAK ELECTROLYTES [J].
EDWARDS, TJ ;
MAURER, G ;
NEWMAN, J ;
PRAUSNITZ, JM .
AICHE JOURNAL, 1978, 24 (06) :966-976