Comparative analysis of isopropyl alcohol dehydration using ionic liquids and deep eutectic solvent

Amit Kumar Gomey , Mata Mani Tripathi , Mohd Belal Haider , Rakesh Kumar
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Abstract

The current article deals with the separation of the azeotropic mixture of isopropyl alcohol (IPA) and water using an ionic liquid, 1-ethyl-3-methylimidazolium tetrafluoroborate ([EMIM][BF4]) and Deep Eutectic Solvents (DESs), Choline Chloride/glycerol (Glyceline) and Choline Chloride/Ethylene Glycol (Ethaline). Conventional dimethyl sulfoxide (DMSO) solvents are used to compare the results for IPA dehydration. Process modelling and simulation were carried out in the Aspen Plus simulator (v.8.6). The NRTL model was used to calculate the thermodynamic properties as well as the vapour-liquid equilibria of the ternary systems. The process parameters such as entrainer flow rate, binary feed stage, entrainer feed stage, column stages, reflux ratio, reboiler and condenser duties were evaluated using sensitivity analysis and design spec tools of the simulator. The industrial process for both systems, containing a separation column and a recovery column, was simulated at a steady state. Both processes were optimised using the optimisation tool of the simulator and compared based on the energy requirement. Further, based on the simulation results, we proposed an alternate process design for solvent recovery using a flash drum. The results show that more than 99.9 mol% IPA purity can be achieved using both ILs as well as DESs. The overall energy requirement for the separation of IPA-water mixture using [EMIM][BF4] entrainer in a conventional process was found to be lower than DMSO. The proposed alternate process further reduces the energy requirement compared to the conventional process for both IL and DESs systems.

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离子液体与深度共熔溶剂脱水异丙醇的比较分析
本文研究了用离子液体1-乙基-3-甲基咪唑四氟硼酸盐([EMIM][BF4])和深共晶溶剂(DESs)、氯化胆碱/甘油(Glyceline)和氯化胆碱/乙二醇(Ethaline)分离异丙醇(IPA)和水的共沸混合物。用传统的二甲亚砜(DMSO)溶剂比较了异丙醇脱水的结果。过程建模和仿真在Aspen Plus模拟器(v.8.6)中进行。采用NRTL模型计算了三元体系的热力学性质和汽液平衡。利用模拟器的灵敏度分析和设计规格工具,对夹带器流量、二元进料级、夹带器进料级、塔级、回流比、再沸器和冷凝器负荷等工艺参数进行了评估。在稳态下模拟了两种系统的工业过程,包括分离塔和回收塔。使用模拟器的优化工具对两个过程进行了优化,并根据能量需求进行了比较。此外,基于模拟结果,我们提出了一种使用闪蒸鼓回收溶剂的替代工艺设计。结果表明,用il和DESs均可获得99.9 mol%以上的IPA纯度。在常规工艺中,使用[EMIM][BF4]夹带剂分离ipa -水混合物所需的总能量低于DMSO。与IL和DESs系统的传统工艺相比,所提出的替代工艺进一步降低了能量需求。
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