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本文以聚醚砜(PES)为膜材料,聚乙烯吡咯烷酮(PVP)、聚乙二醇(PEG)-400为添加剂,N,N-二甲基乙酰胺(DMAC)为溶剂,用非溶剂致相分离法制备了超滤膜——聚醚砜中空纤维超滤膜。通过正交试验法探索喷丝头距离水面的高度、凝固浴的温度、PES浓度、PEG-400浓度等因素对膜性能的影响,同时进一步研究了三个因素对成膜性能的影响规律,分析并确定了制备PES中空纤维超滤膜的最佳实验条件为:喷丝头距离水面的高度20cm,凝固浴温度318K-328K,PES浓度为18%。 相似文献
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提出了一种利用中空纤维膜液液微萃取—高效液相色谱直接测定氢化可的松与蛋白质结合率的新方法.正辛醇相体积小且允许剧烈搅拌,样品消耗量小、时间短,是测定药物蛋白质结合率的好方法. 相似文献
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In an effort to find the effect of mass transfer ,surface tesion and drag forces on the velocity distribution,the mathematical model of the velocity profile of a nascent hollow fiber during membrane formation in the air gap region was numerically simulated by using the Runge-Kutta method (fourth-order method).The effect of mass transfer on velocity distribution based on the complicated function(G(Ch^s))was presented and the dffects of a complicated function were studied in two cases:in the first case,G(Ch^s) was constant;in the second,G(Ch^s) was variable.The latter was done by varying with the concentration of solvent in a nascent hollow fiber through the air-gap region.One empirical equation was used to describe this change and the predected values had a better agreement with the experimental values.To verify the moedl hypotheses,hollow fiber membranes were spun from 20:80 polybenzimidazole/polyetherimide dopes with 25.6 wt% solid in N,N-dimethylacetamide (DMAc) using water as the external and internal coagulants.Based on the experimental results of dry-jet wet-spinning process for the fabrication of hollow fiber membranes,it is found that the model calculated values were in a good agreement with the experimental values. 相似文献
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设计了膜生物反应器 (MBR)与粉末活性炭 (PAC)联合使用的膜组合工艺 (PAC MBR)处理微污染地表水 ,并用分子量分析方法来考察PAC MBR组合工艺及各单元工艺对有机物的去除效果 .分析结果表明 ,由于原水中的小分子有机物难生物降解 ,该工艺出水有机物集中在小于 1k的分子量区间内 ,活性炭的投加能显著提高这部分有机物的去除率 .试验证明 ,PAC MBR工艺中生物处理与活性炭吸附互相促进 ,在稳定运行阶段对CODMn、UV2 54 、UV4 10 和氨氮的去除率分别达到 70 %、70 %、10 0 %和 92 % . 相似文献