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Critical properties and acentric factors of ionic liquids

机译:离子液体的关键特性和偏心因子

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Since most ionic liquids (ILs) decompose before reaching their critical state, the experimental measure ment of their critical properties are not possible. In this study, the critical temperatures, critical pressures and acentric factors of ten commonly investigated ILs were determined by making an optimum fit of the calculated vapor-liquid equilibrium data of binary mixtures of CO_2+IL to the experimental values found in literature. For this purpose, the Peng-Robinson equation of state (PR EoS) and the differential evolution optimization method were used. The ILs considered were 1-ethyl-3-methylimidazolium hexafluorophosphate ([emim][PF_6]), 1-ethyl-3-methylimidazolium bis(tri-fluoromethylsulfonyl) imide ([emim][Tf_2N]), 1-butyl-3-methylimidazolium tetrafluoroborate ([bmim][BF_4]), 1-butyl-3-methylimidazolium hexafluorophosphate ([bmim][PF_6]), 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide ([bmim][Tf_2N]), 1-hexyl-3-methylimidazolium tetrafluoroborate ([hmim][BF_4]), 1-hexyl-3-methylimidazolium hexafluorophosphate ([hmim][PF_6]), 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide ([hmim][Tf_2N]), 1-octyl-3-methylimidazolium tetrafluoroborate ([omim][BF_4]) and 1-octyl-3-methyhrnidazolium hexafluorophosphate ([omim][PF_6]). To evaluate the ability of the determined parameters in predicting the phase behavior of systems other than the systems that were used for parameter optimization, both sets of parameters obtained in this work and that of Valderrama et al. were used to predict bubble-point pressures of CHF_3+[bmim][PF_6] (by using the PR EoS and the Soave-Redlich-Kwong equation of state. The bubble-point pressures of CO_2+IL systems optimized in this study by the PR EoS were also determined using the Soave-Redlich-Kwong equation of state (SRK EoS). In addition, liquid densities of pure ILs were predicted using a generalized correlation proposed by Valderrama and Abu-Shark. In all cases, the various predicted properties of these ten ILs, were in better agreement with the experimental data, using the critical properties and acentric factor obtained in this study, compared to the values suggested by Valderrama et al.
机译:由于大多数离子液体(IL)在达到临界状态之前都会分解,因此无法对其临界性质进行实验测量。在这项研究中,通过将计算得出的CO_2 + IL二元混合物的气液平衡数据与文献中的实验值进行最佳拟合,确定了十种常用的ILs的临界温度,临界压力和无心因素。为此,使用了Peng-Robinson状态方程(PR EoS)和微分进化优化方法。所考虑的IL是1-乙基-3-甲基咪唑鎓六氟磷酸盐([emim] [PF_6]),1-乙基-3-甲基咪唑鎓双(三氟甲基磺酰基)酰亚胺([emim] [Tf_2N]),1-丁基-3-甲基咪唑四氟硼酸酯([bmim] [BF_4]),1-丁基-3-甲基咪唑六氟磷酸盐([bmim] [PF_6]),1-丁基-3-甲基咪唑双(三氟甲基磺酰基)酰亚胺([bmim] [Tf_2N]),1 -己基-3-甲基咪唑四氟硼酸酯([hmim] [BF_4]),1-己基-3-甲基咪唑六氟磷酸盐([hmim] [PF_6]),1-己基-3-甲基咪唑双(三氟甲基磺酰基)酰亚胺([hmim] [ Tf_2N]),1-辛基-3-甲基咪唑四氟硼酸盐([omim] [BF_4])和1-辛基-3-甲基咪唑六氟磷酸盐([omim] [PF_6])。为了评估确定的参数在预测除用于参数优化的系统以外的系统的相位行为方面的能力,在本工作中以及Valderrama等人的研究中获得了两组参数。通过使用PR EoS和Soave-Redlich-Kwong状态方程来预测CHF_3 + [bmim] [PF_6]的气泡点压力。通过PR优化本研究中CO_2 + IL系统的气泡点压力还使用Soave-Redlich-Kwong状态方程(SRK EoS)确定EoS,此外,使用Valderrama和Abu-Shark提出的广义相关性预测纯IL的液体密度。与Valderrama等人建议的值相比,使用本研究中获得的关键特性和偏心因子,这十个IL均与实验数据更好地吻合。

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