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Bioethanol recovery using the pervaporation separation technique

机译:使用全蒸发分离技术回收生物乙醇

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Purpose - The purpose of this paper is to demonstrate applicability of the pervaporation technique for separation ethanol/water mixtures. Design/methodology/approach - For the purposes of membrane material development for pervaporation zeolite filled and unfilled cellulose acetate membranes were prepared. Zeolite types were 4A, 13X. The effect of incorporation of nano-sized zeolites prepared in a colloidal form in membranes was also investigated. Equilibrium sorption experiments were carried out. Degrees of swelling were calculated at different liquid feed mixture compositions for separating an azeotrope forming mixture, ethanol/water by pervaporation. Findings - Zeolite 13X filled CA membrane may have the better pervaporation performance than zeolite 4A filled CA membrane. From the sorption tests it is concluded that ethanol/water azeotropy can be achieved by pervaporation. Practical implications - Application of CA membranes in industrial scale pervaporation units may be feasible for separation of ethanol/water mixtures. Specially ethanol/water azeotropy will be achieved by pervaporation. Using distillation and pervaporation hybrid systems, bioethanol can be produced economically. Orginality/value - The paper illustrates the success of pervaporation techniques in separating ethanol/water mixtures.
机译:目的-本文的目的是证明渗透蒸发技术在分离乙醇/水混合物中的适用性。设计/方法/方法-为了开发用于全蒸发的膜材料,制备了填充和未填充的醋酸纤维素膜。沸石类型为4A,13X。还研究了以胶体形式制备的纳米尺寸沸石掺入膜中的效果。进行平衡吸附实验。在不同液体进料混合物组成下计算溶胀度,以通过共蒸发分离形成共沸混合物的乙醇/水。研究结果-填充13X的CA膜比填充4A的CA膜具有更好的全蒸发性能。从吸附试验得出结论,可以通过全蒸发实现乙醇/水的共沸。实际意义-在工业规模的全蒸发装置中应用CA膜对于分离乙醇/水混合物可能是可行的。特别地,乙醇/水的共沸将通过全蒸发实现。使用蒸馏和全蒸发混合系统,可以经济地生产生物乙醇。原始值/值-本文说明了渗透蒸发技术在分离乙醇/水混合物中的成功。

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