Modelling VLE data of CO2 and H2S in aqueous solutions of N-methyldiethanolamine based on non-random mixing rules

被引:16
作者
Poormohammadian, S. J. [1 ]
Lashanizadegan, Asghar [1 ]
Salooki, Mahdi Koolivand [2 ]
机构
[1] Univ Yasuj, Dept Chem Engn, Yasuj 7591874831, Iran
[2] Res Inst Petr Ind, Gas Res Div, Tehran 146651998, Iran
关键词
CO2 and H2S solubility; Thermodynamic modelling; PR and SRK equations of state; Non-random mixing rule; MDEA-H2O-CO2; system; MDEA-H2O-H2S system; LOCAL COMPOSITION MODEL; EXCESS GIBBS ENERGY; CARBON-DIOXIDE; HYDROGEN-SULFIDE; NATURAL-GAS; SOLUBILITY; EQUATION; ABSORPTION; STATE; MONOETHANOLAMINE;
D O I
10.1016/j.ijggc.2015.07.036
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The vapor liquid equilibrium (VLE) data of carbon dioxide and hydrogen sulfide in N-methyldiethanol-amine (MDEA) solutions has been investigated by Peng-Robinson and Soave-Redlish-Kwong equations of state (EOS). Random and non-random mixing rules have been used for calculating the parameters of the EOS. The predictions of the modelling are compared with the experimental data obtained from the literature for 2 and 4 mole of MDEA per kg of water. It was shown that the data obtained by random mixing rules has 24.7 and 32.5% absolute relative deviation (ARD) for PR and SRK equations of state respectively in calculating the partial pressure of CO2. Also the results had more deviation from the experimental data when binary interaction parameters (k(ij)) added to the random mixing rules. Finally the VLE data of CO2 and H2S is examined by non-random mixing rules and the results were in excellent agreement with the experimental data. The ARD in this case was 3.7 and 6.7% for PR and SRK equations of states respectively in calculating the partial pressure of H2S. The results of the modelling have been compared and discussed with other modelling results such as ePC-SAFC, eNRTL and UNIQUAC models. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:87 / 97
页数:11
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