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络合萃取法处理工业苯胺废水 总被引:16,自引:0,他引:16
依据可逆络合反应萃取的基本原理,通过对苯胺废水的络合萃取相平衡及错流萃取工艺研究,设计了TsH-1络合萃取剂,处理工艺用单一萃取方法可使苯胺废水达标排放。 相似文献
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液膜法处理对硝基苯胺废水的研究 总被引:23,自引:1,他引:23
本文研究了对硝基苯胺水溶液的乳状液膜处理过程,实际工业废水经三级液膜萃取可达到国家排放标准,对硝基苯胺盐在有机膜相的“渗漏”应予注意。 相似文献
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膜萃取过程的传质特性研究 总被引:16,自引:0,他引:16
膜萃取是一种新型的分离技术。本文在中空纤维膜器中研究了膜萃取过程的传质特性。通过四种不同体系的实验,求取了基于水相的总传质系数,提出了求算膜萃取过程中各分传质系数k_(?)、k_(?)、k_(?)的半经验关联式。研究表明,减小膜阻可以强化膜萃取过程,提高过程的总传质系数.比较和分析膜萃取过程中各部分传质阻力,可以看出,对于萃取相平衡常数m1的体系应选用疏水膜器,对于m1体系则应选用亲水膜器。 相似文献
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硅橡胶复合膜处理含酚废水 总被引:8,自引:0,他引:8
采用了一种新的硅橡胶复合中空纤维膜处理苯酚废水。实验中复合膜硅橡胶厚度小于10μm,较前人使用硅橡胶管处理废水时苯酚的透过速率大大加快。处理高浓度(8.977 g/L)和低浓度(0.939 g/L)的苯酚废水时,去除效果分别能达到99.9%和96.9%。通过相应的模型计算,低浓度苯酚传质系数能达到3.92×10-7m/s,比硅橡胶管处理苯酚废水传质系数(1.29×10-7m/s)有很大的提高。实验发现碱液的浓度对苯酚传质系数没有太大的影响,与作者的传质模型比较吻合。也研究了含氯化钠的苯酚的传质,发现氯化钠的存在大大增加了苯酚的传质系数。 相似文献
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采用萃取-H103大孔树脂吸附联合处理苯胺废水,试验了各种条件对废水中COD和苯胺去除率的影响.结果表明,萃取的最佳工艺条件是:甲苯作萃取剂,pH为7.5,萃取剂与废水体积比为1:2,在室温(10℃)下振荡、恒温箱(25℃)中静置各10 min进行二级萃取,废水中COD和苯胺去除率均达到90%以上;以萃取出水作为后续H103大孔树脂吸附柱的进水,当pH为7.5,废水流速以2.5、3.5、4.5 BV·h-1流过吸附柱,出水中COD和苯胺质量浓度降至100 mg·L-1和5 mg·L-1以下,去除率分别达到92%和95%以上. 相似文献
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The membrane extraction experiments were performed with tributyl phosphate/acetic acid (HAc)/water, n-butanol/HAc/water and 20% Alamine (in kerosene); HAc; and water as working systems. HAc was transferred from the aqueous phase to the organic phase. The effect of flat membranes swelling on mass transfer was studied. The membranes were microporous polysulfone and microporous polytetrafluoroethylene. The overall mass transfer coefficients based on the water phase were calculated and compared between nonswollen and swollen membranes. The experimental results show that the physical structure of the flat membranes used in our experiments was changed if soaked by organic solvents; however, change in thickness was not found. The overall mass transfer coefficients clearly were decreased after the flat membranes were swollen. The most likely reason is that the mass transfer resistance was increased because of the change of the membrane structure. The results also show that it is better to choose a hydrophilic membrane to reach high mass transfer performance when the equilibrium constant is very low. © 1999 John Wiley & Sons, Inc. J Appl Polym Sci 73: 1555–1561, 1999 相似文献
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以苯酚为模型污染物,以氢氧化钠溶液为萃取液,利用平板复合膜[聚二甲基硅氧烷(PDMS)/聚偏氟乙烯(PVDF)]构造渗透萃取体系,系统地研究了该体系渗透萃取含酚水溶液的传质过程与特性。探讨了料液与萃取液的浓度及流量、运行温度等操作条件及活性层厚度对渗透萃取传质性能的影响。结果表明,pH>13时,总传质系数Kov不随萃取液流量及浓度变化而变化;苯酚的液膜传质系数kf与膜面流动Reynolds数Re0.46呈正比,传质通量与温度符合Arrhenius方程。在苯酚初始浓度5.0~15.0 g8226;L-1范围内,Kov为定值。活性皮层厚度为4、6、8 μm的膜扩散传质系数分别为15.0×10-7、9.9×10-7及7.5×10-7m8226;s-1(323.2 K),较均质膜提高了2~4倍。苯酚在复合膜中的传质仍属膜阻控制的传质。 相似文献
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新型硅橡胶膜生物反应器用于有机废水处理的膜传质动力学 总被引:9,自引:0,他引:9
用中空纤维型硅橡胶管构造了管束式和卷绕式两种膜器,将它们结合进一个生物反应器系统,用于对废水中的挥发性有机化合物(VOC)进行生物降解处理。本文以甲苯为对象,研究了VOC在这种系统中穿过膜的传质问题。基于液-膜-液的串联阻力概念和质量平衡,构造了一个关于膜总传质系数的简单指数模型,用于传质实验的分析。将甲苯溶于水中模拟有机废水,配制适合于甲苯降解细菌生长的培养液,进行了甲苯从废水穿过膜到培养液中的传质实验,并将细菌移植进培养液进行了生物降解条件下的传质实验。对培养液中细菌存在和不存在两种情况下的甲苯传质实验进行了分析。结果表明,总传质系数的指数模型基本上与实验条件符合,所得到的甲苯的总膜传质系数具有10-6m·s-1数量级,卷绕膜器的总传质系数较管束型的稍高,生物反应条件下的总传质系数又较细菌不存在时的稍高。 相似文献
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David E. Liu Colin Cerretani Rodrigo Tellez Agnes P. Scheer Steve Sciamanna Paul F. Bryan Clayton J. Radke John M. Prausnitz 《American Institute of Chemical Engineers》2015,61(9):2795-2809
Removal of dilute bioproducts from fermenter broths is a major challenge both to avoid microbe inhibition and to recover solutes economically without water loss. We analyze a proposed new process, membrane vapor extraction (MVE), where semi‐volatile dilute aqueous solutes vaporize at the upstream side of an omniphobic, microporous membrane and dissolve into a nonpolar solvent highly favorable to the solutes but not to water. A new membrane‐process analysis is outlined and applied to the countercurrent recovery of 2 wt % aqueous butanol by a prototype solvent (dodecane) at 40°C. Thermodynamic phase equilibria, pioneered by the Prausnitz school, are crucial to MVE process design. Over 90% of the feed butanol is recovered with essentially no water loss giving a separation factor of over 1000. Energy requirements in MVE are low. Our design calculations demonstrate that MVE is a viable separation process to remove and recover dilute aqueous biosolutes. © 2015 American Institute of Chemical Engineers AIChE J, 61: 2795–2809, 2015 相似文献
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In this paper, a new liquid membrane technique, hollow fiber renewal liquid membrane (HFRLM), is presented, which is based on the surface renewal theory, and integrates the advantages of fiber membrane extraction, liquid film permeation and other liquid membrane processes. The results from the system of CuSO4+D2EHPA in kerosene+HCl show that the HFRLM process is very stable. The liquid membrane is renewed constantly during the process, the direct contact of organic droplets and aqueous phase provides large mass transfer area. These effects can significantly reduce the mass transfer resistance in the lumen side. Then the mixture of feed phase and organic phase flowing through the lumen side gives a higher mass transfer rate than that of stripping phase and organic phase, because the aqueous layer diffusion of feed phase is the rate-controlling step. The overall mass transfer coefficient increases with increasing flow rates and D2EHPA concentration in the organic phase, and with decreasing initial copper concentration in the feed phase. The overall mass transfer coefficient also increases with increasing pH in the feed phase, and reaches a maximum value at pH of 4.44, then decreases. Also, there is a favorable w/o volume ratio of 20:1 to 30:1 for this process. Compared with hollow fiber supported liquid membrane and hollow fiber membrane extraction processes, HFRLM process has a high mass transfer rate. Mathematical model for the HFRLM process based on the surface renewal theory is developed. The calculated results are in good agreement with experimental results under the conditions studied. 相似文献