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Modeling vapor-liquid phase equilibria of hydrogen sulfide and water system using a cubic EOS-G(EX) model

机译:立方体EOS-G(EX)模型建模硫化氢和水系统的汽液相平衡

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Vapor-liquid phase equilibria of the H2S-H2O mixture were correlated by use of a cubic EOS-G(EX) over temperature and pressure range of 0.1-30 MPa and 278-627K. Average absolute deviations (AAD%) between the modeling results and the experimental data taken from literature for both the H2S-rich and the aqueous phases were found less than 5%. The new sets of EOS-G(Ex) model parameters for H2S-H2O mixture were evaluated from the experimental data over the above-mentioned temperature and pressure range. The proposed model was compared with the three previous published models and we discussed the advantages and the disadvantages for each of them. This study demonstrated that the advantages of the cubic EOS-G(EX) model in calculating phase equilibria of H2S-H2O mixture over currently available models, especially at high pressures. The hydrate equilibrium, the salt effect, and the chemical reactions in the aqueous phase were not considered during phase equilibrium calculation in this study. (C) 2018 Elsevier B.V. All rights reserved.
机译:通过在0.1-30MPa和278-627K的温度和压力范围内使用立方EOS-G(EX),将H 2 S-H 2 O混合物的蒸汽液相平衡相关。模拟结果与富含H 2 S的文献中的模拟结果和实验数据之间的平均绝对偏差(AAD%)发现小于5%。从上述温度和压力范围内从实验数据评价H2S-H2O混合物的新eos-g(Ex)模型参数。拟议的模型与前一个公布的模型进行了比较,我们讨论了它们每个人的优势和缺点。该研究表明,立方EOS-G(前)模型在目前可用型号上计算H2S-H2O混合物相平衡的相位平衡,尤其是在高压下。本研究期间,在相平衡计算期间,不考虑水合物平衡,盐效应和水相的化学反应。 (c)2018 Elsevier B.v.保留所有权利。

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