Implementation of CPA EoS for simultaneous solubility modeling of CO2 and H2S in ionic liquid [OMIM][Tf2N]

被引:8
作者
Afsharpour, Alireza [1 ]
Kheiri, Alireza [2 ]
机构
[1] Islamic Azad Univ, Qazvin Branch, Young Researchers & Elite Club, Qazvin, Iran
[2] Kalleh Dairy Co, Dept Tech Unit, Amol, Iran
关键词
acid gas solubility; CO2+H2S; ionic liquid; CPA; thermodynamic model; OMIM][Tf2N; phase equilibria; HIGH-PRESSURE MEASUREMENT; EQUATION-OF-STATE; CARBON-DIOXIDE; HYDROGEN; MIXTURES;
D O I
10.1080/10916466.2017.1419484
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
In this study, solubility of pure CO2 and H2S and their mixture in [OMIM][Tf2N] modeled applying CPA EoS. CPA combines the SRK equation with an advanced association term, which is similar to that of SAFT. From a practical point of view, the target in the CPA project was to develop a thermodynamic model capable of describing complex equilibria of mixtures containing polar/associating chemicals through a simple procedure with respect to the SAFT. The AAD% for binary systems, including H2S + IL and CO2 + IL are 6.81, 5.21 respectively. Moreover, AAD% equal to 13.89 was achieved for the ternary system.
引用
收藏
页码:280 / 286
页数:7
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