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Polymer inclusion membranes containing ionic liquids for the recovery of n-butanol from ABE solutions by pervaporation

机译:含有离子液体的聚合物包涵体,通过渗透渗透液从ABE溶液中回收正丁醇

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Making economically competitive technologies for using biofuels as alternatives to move towards a low carbon economy has recently increased the interest of researchers and industry. Biobutanol has a good potential due to its attractive physicochemical properties. It can be produced through the ABE process (acetone-butanol-ethanol) by Clostridium bacteria. However, severe product inhibition, leading to low productivity and low final concentration in the broth, the butanol toxicity to the microorganisms and the high energy consumption are still the main challenges. Pervaporation (PV) is proposed as an efficient alternative to the current separation methods. In PV, the properties of the membrane material dictate the separation of the process for the recovery of butanol. Different polymers and additives are being studied for different membrane characteristics. This work focuses on the fabrication of composite membranes with different polymer/ionic liquid (PEBA/HMImFAP) compositions by the temperature-induced phase-inversion technique (TIPS) to be used in a PV unit to recover butanol from ABE synthetic mixtures. Modeling of mass transfer through the membrane using the resistances-in-series approach was used to find the liquid and membrane resistances. It was seen that the overall resistance decreases as the flow rate increases; regarding the liquid side resistance, it becomes important at smaller flow rates and is almost negligible for flowrates above 4.5 L min(-1). The resistance that exerted the composite polymeric membrane followed this trend acetone > water > ethanol > butanol. Increasing the IL content favours the selective separation towards butanol because of the smaller membrane resistance. Also, adding IL to the membrane at concentration above 20% leads to a worse separation of the components (in terms of separation factor) because of the formation of defects in the polymeric matrix allowing the water to pass through. Finally, running PV experiments under the same operating conditions allowed the comparison of the PSI of the self-made membranes with a commercial membrane, concluding a better performance of the former membranes.
机译:在经济上使用生物燃料制作经济竞争技术,作为走向低碳经济的替代方案最近增加了研究人员和行业的利益。由于其有吸引力的物理化学性质,Biobutanol具有良好的潜力。它可以通过ABE方法(丙酮 - 丁醇 - 乙醇)通过Clostridium细菌生产。然而,严重的产品抑制,导致肉汤中的低生产率和低的最终浓度,对微生物的丁醇毒性和高能量消耗仍然是主要的挑战。提出渗透蒸发(PV)作为当前分离方法的有效替代方案。在PV中,膜材料的性质决定了丁醇回收过程的分离。正在研究不同的聚合物和添加剂,用于不同的膜特性。这项工作侧重于通过温度诱导的相倒置技术(TIPS)用不同聚合物/离子液体(PEBA / HMIMFAP)组合物的复合膜的制造,以便在PV单元中用于回收来自ABE合成混合物的丁醇。使用膜型型抗膜的质量转移建模用于找到液体和膜抗性。有人看出,随着流速的增加,整体电阻降低;关于液体侧电阻,在较小的流速下变得重要,并且对于4.5μlmin(-1)的流量几乎可以忽略不计。施加复合聚合物膜的抗性跟随该趋势丙酮>水>乙醇>丁醇。增加IL含量,因为膜耐膜抗性较小,含有对丁醇的选择性分离。而且,在20%以上的浓度下向膜加入膜导致组分(在分离因子方面)的分离,因为聚合物基质中的缺陷形成允许水通过。最后,在相同的操作条件下运行PV实验允许与商业膜的自制膜的PSI比较,结束前膜的更好性能。

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