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制备了端羟基聚丁二烯-聚氨酯(HTPB-PU)和端羟基聚丁二烯-乙烯基三乙氧基硅烷-聚氨酯(HTPB-VTES-PU)两种聚氨酯膜。采用傅立叶变换红外光谱(FT-IR)、差示扫描量热仪(DSC)和透射电镜(TEM)分析表征了两种膜的结构,结果发现,HTPB-PU有两个玻璃化转变温度,其膜具有一定程度的微相分离结构;HTPB-VTES-PU有三个玻璃化转变温度,相比于HTPB-PU膜,HTPB-VTES-PU膜的微相分离程度更高。两种膜对1%丁醇/水体系渗透汽化分离结果表明,随HTPB-PU膜内异氰酸酯基/羟基(-NCO/-OH)的增加,膜的分离因子增加,丁醇通量略有增加,而总通量下降;对于HTPB-VTES-PU膜,随VTES添加量的增大,膜的丁醇通量略有增加,水通量增加显著,而膜分离因子下降;与HTPB-PU膜相比,HTPB-VTES-PU膜的丁醇通量增加,但分离因子下降。

Hydroxyl-terminated polybutadiene-polyurethane(HTPB-PU) and HTPB-triethoxyvinylsilane-PU(HTPB-VTES-PU) membranes were prepared for pervaporation of n-butanol/water mixtures.The structure of HTPB-PU and HTPB-VTES-PU membranes were characterized by differential scanning calimetry(DSC),transmission electron microscopy(TEM).The results show that the HTPB-PU membrane possess the micro-phase separation structure,and the micro-phase separation structure of the HTPB-VTES-PU membrane is more significant with compared to HTPB-PU membrane.In 1% n-butanol aqueous solution pervaporation,the HTPB-PU membranes show that the separation factor increases continually with increase of the mole ratio of 4,4′-diphenylmethane diisocyanat(MDI)/HTPB(-NCO/-OH),when the ratio of-NCO/-OH is 2,the separation factor and total flux of the HTPB-PU membrane are 42.8 g/m2·h and 38.1 g/m2·h at 60 ℃,respectively.The total flux of the membrane increases,and the separation factor increases slightly followed by a dramatic decrease with the increase of VTES content for the HTPB-VTES-PU membrane.

参考文献

[1] Atsumi S;Cann AF;Connor MR;Shen CR;Smith KM;Brynildsen MP;Chou KJ;Hanai T;Liao JC .Metabolic engineering of Escherichia coli for 1-butanol production.[J].Metabolic engineering,2008(6):305-311.
[2] Izak P;Schwarz K;Ruth W;Bahl H;Kragl U .Increased productivity of Clostridium acetobutylicum fermentation of acetone, butanol, and ethanol by pervaporation through supported ionic liquid membrane[J].Applied Microbiology and Biotechnology,2008(4):597-602.
[3] Arjan Oudshoorn;Luuk A. M. van der Wielen;Adrie J. J. Straathof .Assessment of Options for Selective 1-Butanol Recovery from Aqueous Solution[J].Industrial & Engineering Chemistry Research,2009(15):7325-7336.
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