天然气水合物形成条件下甲烷+甲醇或乙二醇气液平衡计算的敏感性分析

C. Ozigagu, A. Duben
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摘要

Soave-Redlich-Kwong (SRK-EOS)和Peng-Robinson (PR-EOS)状态方程通常用于描述纯物质和混合物的行为,尽管在处理具有高极性和氢键的物质(如水)时存在困难。用它们研究了甲烷+甲醇、单乙二醇(MEG)和三甘醇(TEG)的二元气液平衡(VLE)。这些液体被用来抑制天然气水合物的形成。研究了甲烷-水包合物在283.89 K ~ 323.56 K和5.01 MPa ~ 18.48 MPa条件下形成的条件。甲醇中甲烷的压力被SRK-EOS或PR-EOS高估了两倍。在甲烷+ MEG体系中,除了SRK-EOS计算的MEG中甲烷的最高浓度外,两种状态方程的预测压力一般都小于实验压力。在甲烷+ TEG系统中,两种模型的预测结果接近且趋势相似。由于相对缺乏广泛的甲烷+ TEG实验数据,甲烷+ TEG计算结果的相似性可作为进一步实验研究该体系的基础。
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Sensitivity Analysis of Computations of the Vapor-Liquid Equilibria of Methane + Methanol or Glycols at Gas Hydrate Formation Conditions
The Soave-Redlich-Kwong (SRK-EOS) and Peng-Robinson (PR-EOS) equations of state are used often to describe the behavior of pure substances and mixtures despite difficulties in handling substances, like water, with high polarity and hydrogen bonding. They were employed in studying the binary vapor-liquid equilibria (VLE) of methane + methanol, monoethylene glycol (MEG), and triethylene glycol (TEG). These liquids are used to inhibit the formation of gas hydrates. The investigation focused on the conditions at which methane-water clathrates can form 283.89 K to 323.56 K and 5.01 MPa to 18.48 MPa. The pressure of methane in methanol is overestimated by a factor of two by either the SRK-EOS or the PR-EOS. In the methane + MEG system, the predicted pressures for both equations of state are generally less than experimental pressure except for the highest concentration of methane in MEG calculated by the SRK-EOS. In the methane + TEG system, the predictions of both models are close and trend similarly. Because of the comparative lack of extensive experimental methane + TEG data, the similarity of the methane + TEG computed results can be used as a basis for further study of this system experimentally.
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