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Vapor–Liquid Equilibria of the CH4 + CO2 + H2S Ternary System with Two Different Global Compositions: Experiments and Modeling
Journal of Chemical & Engineering Data ( IF 2.6 ) Pub Date : 2020-03-06 , DOI: 10.1021/acs.jced.9b01082
Pascal Theveneau 1 , Xiaochun Xu 2 , Olivier Baudouin 3 , Jean-Noël Jaubert 2 , Paola Ceragioli 4 , Christophe Coquelet 1
Affiliation  

The vapor–liquid equilibrium for two mixtures containing methane, carbon dioxide, and hydrogen sulfide was determined experimentally by a static-analytic method. Thirty-one data points were acquired for a range of temperatures from 243 to 333 K at pressures up to 11 MPa. The measured data were correlated with the Peng–Robinson equation of state (EoS) and different mixing rules, which led to the conclusion that a cubic EoS could simultaneously predict the existence of a three-phase region and two critical points on the constant-composition, two-phase boundary curve.

中文翻译:

具有两种不同全局组成的CH 4 + CO 2 + H 2 S三元体系的汽液平衡:实验和建模

通过静态分析方法,通过实验确定了含有甲烷,二氧化碳和硫化氢的两种混合物的气液平衡。在高达11 MPa的压力下,从243到333 K的温度范围内采集了31个数据点。实测数据与Peng-Robinson状态方程(EoS)和不同的混合规则相关,从而得出结论,三次EoS可以同时预测恒组成上三相区域和两个临界点的存在。 ,两相边界曲线。
更新日期:2020-04-24
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