Amine volatility in CO2 capture

被引:164
作者
Nguyen, Thu [1 ]
Hilliard, Marcus [2 ]
Rochelle, Gary T. [1 ]
机构
[1] Univ Texas Austin, Dept Chem Engn, Austin, TX 78712 USA
[2] Dow Chem Co USA, Midland, MI 48674 USA
关键词
Amine volatility; Monoethanolamine; Piperazine; n-Methyldiethanolamine; Ethylenediamine; 2-Amino-2-methyl-1-propanol; VAPOR-LIQUID-EQUILIBRIA; BINARY; WATER; MONOETHANOLAMINE; SOLUBILITY; MIXTURES;
D O I
10.1016/j.ijggc.2010.06.003
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Amine volatility is a key screening criterion for amines to be used in CO2 capture. Excessive volatility may result in significant economic losses and environmental impact. It also dictates the capital cost of the water wash. This paper reports measured amine volatility in 7 m MEA (monoethanolamine), 8 m PZ (piperazine), 7 m MDEA (n-methyldiethanolamine)/2 m PZ (piperazine), 12 m EDA (ethylenediamine), and 5 m AMP (2-amino-2-methyl-1-propanol) at 40-60 degrees C with lean and rich loadings giving CO2 partial pressures of 0.5 and 5 kPa at 40 degrees C. The amine concentrations were chosen to maximize CO2 capture capacity at acceptable viscosity. At the lean loading condition (where volatility is of greatest interest), the amines are ranked in order of increasing volatility: 7 m MDEA/2 m PZ (6/2 ppm), 8 m PZ (8 ppm), 12 m EDA (9 ppm), 7 m MEA (31 ppm), and 5 m AMP (112 ppm). The apparent amine partial molar excess enthalpies in these systems were estimated to range from similar to 10 to 87 kJ/mol of amine. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:707 / 715
页数:9
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