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Blended chitosan and poly (vinyl alcohol) membranes for the prevaporation of methanol and methyl tert-butyl ether

机译:壳聚糖和聚乙烯醇共混膜用于甲醇和甲基叔丁基醚的预蒸发

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摘要

In this research project, blended chitosan/poly(vinyl alcohol) (PVA) membranesudwere produced by mixing PVA and chitosan solutions. Chitosan (CS) was firstuddissolved in acetic acid aqueous solution before PVA solution was added. The mixtureudwas then cured at room temperature. The modified composite membrane was preparedudby coating the mixture of chitosan and PVA solution onto the porous polysulfoneudmembrane by the solution casting technique. The porous polysulfone substrate wasudprepared via phase inversion process from a casting solution containing 12 wt%udpolysulfone, 11 wt% polyethylene glycol and 77 wt% N,N- dimethylacetamide. Theudweight percent of chitosan in the membrane was varied from 20 wt. % to 100 wt. %udwhile the membrane thickness was in the range of 15-30 μm. The unmodified andudmodified composite membranes with PVA were used in pervaporation separation ofudmethanol/methyl-tert-butyl ether (MTBE) mixture. The swelling degree and the totaludflux increased with increasing chitosan content in the membranes. 30 wt. % of methanolud(MeOH) in feed was chose since it gave the optimal overall pervaporation characteristicsudin terms of flux and separation factor. The membrane containing chitosan 20 wt. % toud40 wt. % performed the best. At operating temperature of 50 oC for 20 wt % to 40 wt %udof chitosan, the fluxes obtained are at 52.28 g/m2.hr and 66.92 g/m2.hr with theudseparation factors of 81.00 and 53.22 respectively. The effect of temperature on fluxudfollowed the Arrhenius relationship. The membrane showed excellent performance forudseparation of MeOH/MTBE mixture when the quantity of MeOH in feed is small. It is audvery suitable process for the recovery purpose in order to remove excess MeOH in theudMTBE system.
机译:在该研究项目中,通过混合PVA和壳聚糖溶液生产了壳聚糖/聚乙烯醇(PVA)混合膜。在加入PVA溶液之前,首先将壳聚糖(CS)溶解在乙酸水溶液中。然后将混合物在室温下固化。通过溶液浇铸技术将壳聚糖和PVA溶液的混合物涂覆到多孔聚砜/ udmbrane上来制备改性复合膜。多孔聚砜基材是通过相转化法由包含12wt%udud砜,11wt%聚乙二醇和77wt%N,N-二甲基乙酰胺的流延溶液制备的。膜中壳聚糖的重量百分数为20重量%。 %至100 wt。膜厚度在15-30μm的范围内。将具有PVA的未改性和未改性的复合膜用于全蒸发分离甲醇/甲基叔丁基醚(MTBE)混合物。溶胀度和总流出量随着膜中壳聚糖含量的增加而增加。 30重量选择进料中甲醇的百分比 ud(MeOH),因为它提供了最佳的总渗透蒸发特性以通量和分离因子表示的ud。含有壳聚糖20重量%的膜。 %至 ud40 wt。 %表现最佳。在50°C的操作温度下,壳聚糖的重量百分比为20%至40%时,得到的通量分别为52.28 g / m2.hr和66.92 g / m2.hr,分离系数分别为81.00和53.22。温度对通量的影响遵循Arrhenius关系。当进料中的MeOH量很少时,该膜表现出出色的MeOH / MTBE混合物分离性能。这是一种非常适合回收目的的方法,目的是去除udMTBE系统中的过量MeOH。

著录项

  • 作者

    Mohd. Sakri Norhaslina;

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  • 年度 2009
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  • 原文格式 PDF
  • 正文语种 en
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