乳状液膜法治理H酸生产废水的研究

研究了以三辛胺(TOA)为流动载体的乳状液膜法提取对H酸的最优膜配方及工艺条件,并以实际工业废水进行验证。考察了膜相表面活性剂浓度、载体浓度、外水相pH值、乳水比、内水相浓度对水中COD值去除的影响。通过正交试验,结果表明:以质量分数为3%的聚胺型表面活性剂,体积分数为4%的TOA,质量分数10%的内水相NaOH溶液,油内比Roi为2∶1的乳状液膜体系,处理初始浓度为50 000 mg/L H酸废水,在pH值为3,乳水比Rew为1∶5的传质条件下,对含H酸废水的COD去除率可达90%以上。     

静电纺PA6/PET复合膜的制备及其空气过滤性能

主要研究静电纺纳米/微米纤维复合膜(PA6/PET)的制备及其空气过滤性能,电纺了几种不同密集度的复合膜,研究了其对氯化钠粒子在特定条件下的过滤能力,进行了加载过滤测试,并通过扫描电子显微镜(SEM)对过滤前后纤维膜的表面形态进行观察.结果表明,对于多分散的NaCl粒子来说,过滤材料的过滤效率随着过滤时间的增加而增加.当增大过滤粒子流量时,过滤阻力与流量呈现线性增长关系,但是过滤效率变化不大.本实验中复合膜的最低过滤效率为99.990%.     

中空纤维膜辅助离子液体液相微萃取-高效液相色谱法测定环境水体中的水杨酸

分别以l-辛基-3-甲基咪唑六氟磷酸离子液体([C8MIM][PF6])和三辛基氧化膦(TOPO)作为萃取剂与辅助萃取剂,建立了中空纤维膜辅助的两相液液微萃取-高效液相色谱测定环境水体中水杨酸(Salicylicacid,SA)的新方法.通过对中空纤维膜种类、萃取剂、供体相体积、供体相pH、离子强度和萃取时间相关参数进行优化,获得了较高的富集倍数(1653倍).方法的检出限为0.1μg.L-1,线性范围为0.5—1000μg.L-1.方法对实际样品的加标回收率为89.6%—102.4%,可应用于环境水体中痕量SA的测定.     

废水处理系统中生物聚集体胞外多聚物研究进展

胞外多聚物(Extracellular polymeric substances,EPS)是废水生物处理系统中生物聚集体(包括絮体污泥、生物膜、颗粒污泥等)的重要组成部分,直接包裹于微生物细胞壁外,其理化性质及所处的特殊位置决定了它在生物聚集体中的重要作用.综述了EPS对废水生物处理系统污泥沉降性能、脱水性以及膜生物反应器膜污染影响的相关研究,分析认为EPS组成与结构特性改变污泥表面电位、疏水性等,进而影响污泥沉降与脱水性能、膜污染程度;以好氧颗粒污泥为典型的生物聚集体代表,总结了EPS组分含量与分布对颗粒污泥的形成与结构稳定性的影响,并在EPS提取方法标准化、现代理化技术与分子生物学技术综合分析等方面进行了展望,进一步的研究有望揭示生物絮凝体形成过程EPS的产生与调控机制.     

新型膜分离技术及其工业中的应用

用膜法来处理废水有高效、低能耗和易操作处理效率高的优点,而且有利于回收废液中的物质,在水处理中有着广阔的应用前景.在介绍常规和新型膜分离技术的基础上,对新型膜分离技术在工业中的发展及应用进行了综述.     

地表臭氧增加对黄花夹竹桃和芒果叶片膜脂过氧化程度和保护酶活性的影响

以黄花夹竹桃（Thevetia peruviana（Pers.）k.Schum.）和芒果（Mangifera indica L.）苗木为材料,研究4种臭氧（O3）体积分数[环境大气NF,φ（O3）=10×10-9~20×10-9;低体积分数处理E50,φ（O3）=50×10-9;中体积分数处理E100,φ（O3）=100×10-9;高体积分数处理E200,φ（O3）=200×10-9]下两种植物叶片膜脂过氧化程度、可溶性蛋白质质量分数、可溶性糖质量分数和保护酶活性的变化情况,旨在揭示地表臭氧体积分数升高条件下2种植物生理代谢活动变化机理及响应规律。结果表明：随臭氧体积分数的增加,2种植物丙二醛含量和膜透性均逐渐上升,且与臭氧体积分数呈显著正相关关系,说明两种植物膜脂过氧化程度加剧;低体积分数O3处理时两种植物可溶性蛋白质量分数均逐渐下降,高φ（O3）处理后小幅回升;黄花夹竹桃可溶性糖质量分数逐渐下降,芒果先上升后下降;2种植物的POD活性均显著上升,但上升幅度有较大差异;2种植物的CAT活性均呈先升高再降低的趋势。研究表明,不同体积分数的臭氧暴露下,黄花夹竹桃和芒果均受到不同程度的伤害,芒果对臭氧表现出较强的抗性,黄花夹竹桃对臭氧较敏感。     

光催化膜反应器的设计及其在水处理中的应用

作为一种新型的水处理装置,光催化膜反应器具有反应迅速、降解效率高、降解彻底、无二次污染等特点,在节水减排、微污染水处理、中水回用等方面具有重要的应用价值。总结目前国内外各种不同类型的光催化膜反应器的设计、特点及在水处理中的应用情况,并对其今后的发展提出建议。     

混凝-膜过滤中滤饼层对双酚A的去除强化作用研究

以聚合氯化铝(PAC)和氯化铁(FeCl3)为混凝剂,分析了双酚A(BPA)在1g/L高岭土溶液混凝过程中的特征.并借助循环错流过滤强化污染层累积的方法,评价产生滤饼层的微滤(MF)膜对BPA的截留效果.结果表明:清洁的微滤膜过滤BPA溶液在短时间内达到截留吸附饱和,之后其对BPA的吸附截留作用显著降低;混凝絮体混合液经膜过滤时产生的污染层有利于BPA的去除,且单独混凝对BPA去除率最高的混凝剂投加量下进行膜过滤时的阻力较小.PAC混凝—膜过滤后BPA去除率比单独混凝提高了34.30%;FeCl3混凝—膜过滤后BPA去除率比单独混凝提高了28.38%.初始BPA浓度对混凝-膜过滤去除率有一定影响,BPA浓度为100μg/L时,比BPA浓度为5mg/L时采用2种混凝-微滤膜过滤方式去除率均有提高.     

Effect of iron addition on the performance of anoxic-oxic membrane process and biological phosphorus removal北大核心CSCD

In order to solve the problem of poor treatment of phosphorus in membrane bioreactor (MBR) with long sludge retention time (SRT), a ferric salt was added to enhance phosphorus removal; FeCl36H2O (Fe/P = 2.0) was added to the reactor. The removal efficiency of nitrogen, organic matters, and phosphorus in the MBR was investigated systematically. Moreover, this study focused on the membrane performance, the change of active sludge flora, and the effect of adding a ferric salt on membrane fouling before and after the addition. It was seen that adding the ferric salt could not affect the removal of COD and NH4 +-N and the removal rate of COD and NH4 +-N reached over 90%. However, the average removal rate of phosphorus was 52%, while the removal rate increased by nearly 40% after adding the ferric salt. The effects of adding ferric salts on the dominant bacteria and biological phosphorus removal of activated sludge were further studied. The results showed that the addition of ferric salt (Fe/P = 2.0) decreased the diversity of active sludge flora and relative abundance of some phosphorusaccumulating organisms and had a negative effect on biological phosphorus removal. The analysis of transmembrane pressure difference (TMP) recording revealed that the concentration of iron salts did not exacerbate membrane fouling. The results showed that the concentration of iron salts entering the membrane bioreactor would reduce the relative abundance and phosphorus removal efficiency of the activated sludge in the system to a certain extent, but it had no obvious effect on membrane fouling. It allowed the effluent to attain acceptable standards, especially with respect to phosphorus removal efficiency. © 2018 Science Press. All rights reserved.     

Energy reduction of a submerged membrane bioreactor using a polytetrafluoroethylene (PTFE) hollow-fiber membrane

The fiber length and packing density of the PTFE membrane element were increased. The MBR was stably operated under an SAD^m of 0.13 m³·m^-2·hr^-1. Specific energy consumption was estimated to be less than 0.4 kWh·m^-3. In this study, we modified a polytetrafluoroethylene (PTFE) hollow-fiber membrane element used for submerged membrane bioreactors (MBRs) to reduce the energy consumption during MBR processes. The high mechanical strength of the PTFE membrane made it possible to increase the effective length of the membrane fiber from 2 to 3 m. In addition, the packing density was increased by 20% by optimizing the membrane element configuration. These modifications improve the efficiency of membrane cleaning associated with aeration. The target of specific energy consumption was less than 0.4 kWh·m^-3 in this study. The continuous operation of a pilot MBR treating real municipal wastewater revealed that the MBR utilizing the modified membrane element can be stably operated under a specific air demand per membrane surface area (SAD_m) of 0.13 m³·m^-2·hr^-1 when the daily-averaged membrane fluxes for the constant flow rate and flow rate fluctuating modes of operation were set to 0.6 and 0.5 m³·m^-2·d^-1, respectively. The specific energy consumption under these operating conditions was estimated to be less than 0.37 kWh·m^-3. These results strongly suggest that operating an MBR equipped with the modified membrane element with a specific energy consumption of less than 0.4 kWh·m^-3 is highly possible.