Solubility of CO2 in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation
Chemical Engineering Thermodynamics|Updated:2026-01-06
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Solubility of CO2 in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation
Solubility of CO2 in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation
中国化学工程学报(英文版)2022年41卷第1期 页码:441-448
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School of Chemical and Pharmaceutical Engineering, Hebei University of Science and Technology,Shijiazhuang,China,050018
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纸质出版:2022
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Yu Dong, Tiantian Ping, Shufeng Shen. Solubility of CO2 in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation[J]. 中国化学工程学报(英文版), 2022,41(1):441-448.
in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation[J]. 中国化学工程学报, 2022, 41(1): 441-448.
Yu Dong, Tiantian Ping, Shufeng Shen. Solubility of CO2 in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation[J]. 中国化学工程学报(英文版), 2022,41(1):441-448.DOI:
in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation[J]. 中国化学工程学报, 2022, 41(1): 441-448.DOI:
Solubility of CO2 in nonaqueous system of 2-(butylamino)ethanol with 2-butoxyethanol: Experimental data and model representation
Nonaqueous amine-based system is an attractive solution to overcome high-energy-intensive CO
2
capture process using the conventional aqueous amines. Advanced nonaqueous absorbent of 2- (butylamino)ethanol (BAE) with 2-butoxyethanol (2-BE) has been recently proposed for low-energyconsumption CO
2
capture. In this work
Henry’s law constants of CO
2
in the BAE/2-BE blend were obtained by N
2
O/CO
2
analogy
and correlated in the temperature range of (283–333) K. Vapor-liquid equilibrium (VLE) data for the BAE + CO
2
+ 2-BE system at 65.4% (mass) BAE were also determined in a stirred equilibrium cell at temperatures of (313–393) K and CO
2
partial pressures up to 275 kPa. A single apparent equilibrium constant
K
CO
2
app
was proposed for this system and correlated as a function of temperature
carbonated degree of amine and CO
2
loading. Solubility data were well represented by the modified Kent-Eisenberg model with an average absolute relative deviation (AARD) of 13%.
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