Abejón Ricardo, Saidani Hafedh, Deratani André, Richard Christophe, Sánchez-Marcano José
Institut Européen des Membranes UMR 5635, CNRS, ENSCM, Université de Montpellier, CC 047, Place Eugène Bataillon, 34095 Montpellier, France.
Department of Chemical and Biomolecular Engineering, University of Cantabria, Avda. Los Castros s/n, 39005 Santander, Cantabria, Spain.
Membranes (Basel). 2019 Nov 26;9(12):158. doi: 10.3390/membranes9120158.
Sweeping gas membrane distillation (SGMD) is a useful option for dehydration of aqueous solvent solutions. This study investigated the technical viability and competitiveness of the use of SGMD to concentrate aqueous solutions of 1,3-dimethyl-2-imidazolidinone (DMI), a dipolar aprotic solvent. The concentration from 30% to 50% of aqueous DMI solutions was attained in a bench installation with Liqui-Cel SuperPhobic hollow-fiber membranes. The selected membranes resulted in low vapor flux (below 0.15 kg/h·m) but were also effective for minimization of DMI losses through the membranes, since these losses were maintained below 1% of the evaporated water flux. This fact implied that more than 99.2% of the DMI fed to the system was recovered in the produced concentrated solution. The influence of temperature and flowrate of the feed and sweep gas streams was analyzed to develop simple empirical models that represented the vapor permeation and DMI losses through the hollow-fiber membranes. The proposed models were successfully applied to the scaling-up of the process with a preliminary multi-objective optimization of the process based on the simultaneous minimization of the total membrane area, the heat requirement and the air consumption. Maximal feed temperature and air flowrate (and the corresponding high operation costs) were optimal conditions, but the excessive membrane area required implied an uncompetitive alternative for direct industrial application.
吹扫气膜蒸馏(SGMD)是一种用于脱水溶剂水溶液的有效方法。本研究调查了使用SGMD浓缩1,3 - 二甲基 - 2 - 咪唑啉酮(DMI,一种偶极非质子溶剂)水溶液的技术可行性和竞争力。在配备Liqui - Cel超疏水中空纤维膜的实验室装置中,实现了将DMI水溶液从30%浓缩至50%。所选的膜导致蒸汽通量较低(低于0.15 kg/h·m),但对于使DMI透过膜的损失最小化也很有效,因为这些损失保持在蒸发水通量的1%以下。这意味着进料到系统中的DMI超过99.2%在产生的浓缩溶液中得以回收。分析了进料和吹扫气流的温度及流速的影响,以建立简单的经验模型来表示蒸汽透过中空纤维膜的情况以及DMI的损失。所提出的模型成功应用于该过程的放大,基于同时最小化总膜面积、热量需求和空气消耗对该过程进行了初步的多目标优化。最高进料温度和空气流速(以及相应的高运行成本)是最优条件,但所需的过大膜面积意味着对于直接工业应用而言是一种缺乏竞争力的选择。