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Thermodynamic and Process Analyses of Extractive Distillation for Separating Refrigerant R-410A Using Imidazolium-Cyano-Based Ionic Liquids
Industrial & Engineering Chemistry Research ( IF 3.8 ) Pub Date : 2024-12-24 , DOI: 10.1021/acs.iecr.4c03268 Julia E. Espinoza Mejia, Abdulrhman M. Arishi, Mark B. Shiflett, Aaron M. Scurto
Industrial & Engineering Chemistry Research ( IF 3.8 ) Pub Date : 2024-12-24 , DOI: 10.1021/acs.iecr.4c03268 Julia E. Espinoza Mejia, Abdulrhman M. Arishi, Mark B. Shiflett, Aaron M. Scurto
R-410A is a near-azeotropic refrigerant mixture of difluoromethane (HFC-32) and pentafluoroethane (HFC-125) that is scheduled to be phased out internationally due to a high Global Warming Potential (GWP). While conventional distillation cannot be used, extractive distillation using ionic liquids (ILs) has been proposed to separate and recycle HFC-32 (lower GWP) for future refrigerant blends and to repurpose HFC-125 (high GWP). Here, we present both a thermodynamic and process design analyses of various ILs using an equation of state method. From experimental binary vapor–liquid equilibrium data and equation of state modeling, 1-ethyl-3-methylimidazolium tricyanomethanide [C2C1im][tcm] and 1-ethyl-3-methylimidazolium dicyanamide [C2C1im][dca] were identified from 10 ILs as viable entrainers. Selectivity increases with temperature and decreases with pressure, while the solvent-to-feed (S/F) ratio did not have much effect. These effects were more pronounced for [C2C1im][tcm] than for [C2C1im][dca]. A sensitivity analysis reveals that the optimum operational parameters were solvent-to-feed ratio (S/F), reflux ratio (RR), and total number of stages (Nt) with values of 5, 3, and 20, respectively, for the case of [C2C1im][tcm] and 6, 3, and 20 for [C2C1im][dca]. High-purity products HFC-32 and HFC-125 (>99.5 wt %) were obtained with IL [C2C1im][tcm], providing the lowest energy consumption, compared to [C2C1im][dca] and other ILs.
中文翻译:
使用咪唑氰离子液体分离制冷剂 R-410A 的萃取蒸馏的热力学和过程分析
R-410A 是二氟甲烷 (HFC-32) 和五氟乙烷 (HFC-125) 的近共沸制冷剂混合物,由于全球变暖潜能值 (GWP) 高,计划在国际上逐步淘汰。虽然不能使用常规蒸馏法,但已经提出了使用离子液体 (IL) 的萃取蒸馏法,以分离和回收 HFC-32(较低的 GWP)用于未来的制冷剂混合物,并重新利用 HFC-125(高 GWP)。在这里,我们使用状态方程法对各种 IL 进行了热力学和过程设计分析。从实验二元气液平衡数据和状态方程建模中,从 10 种 IL 中鉴定出 1-乙基-3-甲基咪唑鎓三氰化物 [C2C1im][tcm] 和 1-乙基-3-甲基咪唑鎓二氰胺 [C2C1im][dca] 为活的夹带剂。选择性随温度升高而降低,而溶剂与进料 (S/F) 的比率影响不大。[C2C1im][tcm] 的这些影响比 [C2C1im][dca] 更明显。敏感性分析显示,最佳操作参数为溶剂进料比 (S/F)、回流比 (RR) 和总级数 (Nt),对于 [C2C1im][tcm] 和 6、3 和 20,对于 [C2C1im][dca]。与 [C2C1im][dca] 和其他 IL 相比,IL [C2C1im][tcm] 获得了高纯度产品 HFC-32 和 HFC-125 (>99.5 wt %),提供了最低的能耗。
更新日期:2024-12-24
中文翻译:
使用咪唑氰离子液体分离制冷剂 R-410A 的萃取蒸馏的热力学和过程分析
R-410A 是二氟甲烷 (HFC-32) 和五氟乙烷 (HFC-125) 的近共沸制冷剂混合物,由于全球变暖潜能值 (GWP) 高,计划在国际上逐步淘汰。虽然不能使用常规蒸馏法,但已经提出了使用离子液体 (IL) 的萃取蒸馏法,以分离和回收 HFC-32(较低的 GWP)用于未来的制冷剂混合物,并重新利用 HFC-125(高 GWP)。在这里,我们使用状态方程法对各种 IL 进行了热力学和过程设计分析。从实验二元气液平衡数据和状态方程建模中,从 10 种 IL 中鉴定出 1-乙基-3-甲基咪唑鎓三氰化物 [C2C1im][tcm] 和 1-乙基-3-甲基咪唑鎓二氰胺 [C2C1im][dca] 为活的夹带剂。选择性随温度升高而降低,而溶剂与进料 (S/F) 的比率影响不大。[C2C1im][tcm] 的这些影响比 [C2C1im][dca] 更明显。敏感性分析显示,最佳操作参数为溶剂进料比 (S/F)、回流比 (RR) 和总级数 (Nt),对于 [C2C1im][tcm] 和 6、3 和 20,对于 [C2C1im][dca]。与 [C2C1im][dca] 和其他 IL 相比,IL [C2C1im][tcm] 获得了高纯度产品 HFC-32 和 HFC-125 (>99.5 wt %),提供了最低的能耗。