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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Phase Equilibrium Data of Gas Hydrates Formed from a CO2 + CH4 Gas Mixture in the Presence of Tetrahydrofuran
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Phase Equilibrium Data of Gas Hydrates Formed from a CO2 + CH4 Gas Mixture in the Presence of Tetrahydrofuran

机译:四氢呋喃存在下由CO2 + CH4气体混合物形成的气体水合物的相平衡数据

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摘要

In this work, the phase equilibrium conditions for gas hydrates formed from a CO2/CH4 gas mixture (0.4 CO2 and 0.6 CH4 in mole fraction) in the presence tetrahydrofuran (THF) were measured using the isothermal pressure search method and reported. The THF mole fractions used were 0.005, 0.01, 0.03, and 0.05 respectively. It was found that the equilibrium hydrate formation conditions obtained in the presence of THF shifted to high temperatures and low pressures as compared with those obtained using the same gas mixture in pure water. For the hydrates formed at a given temperature, the phase equilibrium pressure was observed to decrease as the THF mole fraction increased from 0.005 to 0.05. Therefore, it was confirmed that THF can be used as an effective thermodynamic promoter for CO2 separation from the CO2/CH4 gas mixture by hydrate formation. The heat of hydrate dissociation was also determined based on the measured phase equilibrium data of the gas hydrates formed from the CO2/CH4 gas mixture in the presence of THF. It was found that structure II hydrate was formed from the CO2/CH4 gas mixture in the presence of THF. Then the impact of driving force on CO2 separation from the CO2/CH4 gas mixture was investigated. The results indicated that the competition between CO2 and CH4 molecules for hydrate cage occupancy became stronger with the increase of driving force. Thus, a lower pressure at the given temperature is preferred for CO2 separation from the CO2/CH4 gas mixture by hydrate formation in the presence of THF.
机译:在这项工作中,使用等温压力搜索方法测量了在四氢呋喃(THF)存在下由CO2 / CH4气体混合物(摩尔分数为0.4 CO2和0.6 CH4)形成的气体水合物的相平衡条件,并进行了报道。使用的THF摩尔分数分别为0.005、0.01、0.03和0.05。发现与在纯水中使用相同气体混合物获得的平衡水合物形成条件相比,在THF存在下获得的平衡水合物形成条件转移至高温和低压。对于在给定温度下形成的水合物,观察到相平衡压力随着THF摩尔分数从0.005增加到0.05而降低。因此,证实了THF可以用作通过水合物形成从CO 2 / CH 4气体混合物中分离CO 2的有效热力学促进剂。还基于在THF存在下由CO 2 / CH 4气体混合物形成的气体水合物的测得的相平衡数据来确定水合物的解离热。发现在THF存在下由CO 2 / CH 4气体混合物形成结构II水合物。然后研究了驱动力对从CO2 / CH4气体混合物中分离CO2的影响。结果表明,随着驱动力的增加,CO2和CH4分子在水合物笼中的竞争加剧。因此,优选在给定温度下的较低压力,以在THF存在下通过水合物形成从CO 2 / CH 4气体混合物中分离CO 2。

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