浓度极化对聚癸基/丙烯酸五氟丙基甲基硅氧烷共聚物复合膜渗透汽化分离正丁醇的影响

IF 1.6 Q4 CHEMISTRY, PHYSICAL
T. N. Rokhmanka, G. S. Golubev, E. A. Grushevenko, I. L. Borisov
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引用次数: 0

摘要

研究了聚十二烷基甲基硅氧烷和聚甲基五氟丙基硅氧烷共聚物(50F5)选择性层复合膜在渗透汽化回收正丁醇过程中的传输和分离特性。结果表明,具有选择性共聚物(M-50F5)层的膜对正丁醇/水具有较高的分离系数(35),总渗透通量为0.31 kg/(m2 h)。首次分析了浓度极化对模型发酵混合物正丁醇回收效率的影响,包括浓度极化模量和扩散边界层厚度的计算。结果表明,将进料混合物的流速提高到30 cm/s以上,可以消除浓度极化效应,边界层厚度减小到零。流体动力学体系的优化允许由浓度极化引起的传质限制最小化,特别是在低丁醇浓度下。所得结果证实了使用50f5基膜从发酵液中渗透蒸发回收丁醇的潜力,并为改进多组分系统的分离技术开辟了新的机会。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Effect of Concentration Polarization in the Pervaporation Separation of n-Butanol through a Composite Membrane Based on Poly(decyl/pentafluoropropyl acrylate)methylsiloxane Copolymer

Effect of Concentration Polarization in the Pervaporation Separation of n-Butanol through a Composite Membrane Based on Poly(decyl/pentafluoropropyl acrylate)methylsiloxane Copolymer

Effect of Concentration Polarization in the Pervaporation Separation of n-Butanol through a Composite Membrane Based on Poly(decyl/pentafluoropropyl acrylate)methylsiloxane Copolymer

The transport and separation characteristics of the composite membrane with a selective layer based on a copolymer of polydecylmethylsiloxane and polymethylpentafluoropropylsiloxane (50F5) were studied during the pervaporation recovery of n-butanol from aqueous mixtures. It was shown that the membrane with the selective layer of copolymer (M-50F5 exhibits a high separation factor for n-butanol/water (35) and a total permeate flux of 0.31 kg/(m2 h). For the first time, an analysis of the impact of concentration polarization on the efficiency of n-butanol recovery from a model fermentation mixture was conducted, including the calculation of the concentration polarization modulus and the thickness of the diffusion boundary layer. It was revealed that increasing the flow rate of the feed mixture above 30 cm/s eliminates concentration polarization effects, as evidenced by a reduction in the boundary layer thickness to zero. Optimization of the hydrodynamic regime allowed for the minimization of mass transfer limitations caused by concentration polarization, particularly at low butanol concentrations. The obtained results substantiate the potential of using 50F5-based membranes for the pervaporation recovery of butanol from fermentation broths and open new opportunities for improving separation technologies for multicomponent systems.

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来源期刊
CiteScore
3.10
自引率
31.20%
发文量
38
期刊介绍: The journal Membranes and Membrane Technologies publishes original research articles and reviews devoted to scientific research and technological advancements in the field of membranes and membrane technologies, including the following main topics:novel membrane materials and creation of highly efficient polymeric and inorganic membranes;hybrid membranes, nanocomposites, and nanostructured membranes;aqueous and nonaqueous filtration processes (micro-, ultra-, and nanofiltration; reverse osmosis);gas separation;electromembrane processes and fuel cells;membrane pervaporation and membrane distillation;membrane catalysis and membrane reactors;water desalination and wastewater treatment;hybrid membrane processes;membrane sensors;membrane extraction and membrane emulsification;mathematical simulation of porous structures and membrane separation processes;membrane characterization;membrane technologies in industry (energy, mineral extraction, pharmaceutics and medicine, chemistry and petroleum chemistry, food industry, and others);membranes and protection of environment (“green chemistry”).The journal has been published in Russian already for several years, English translations of the content used to be integrated in the journal Petroleum Chemistry. This journal is a split off with additional topics.
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