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1.
氯化铁絮凝法减轻膜污染 总被引:12,自引:0,他引:12
采用氯化铁絮凝法去除膜生物反应器混合液中难降解的大分子有机物,确定Fe^3 的最佳投加量为60mg/L,该工艺可显著降低混合液中CODCr,减轻膜污染,并且对膜生物反应器中的生物相活性没有影响。 相似文献
2.
生物陶粒柱—PAC—膜过滤装置系统处理饮用水实验研究 总被引:2,自引:0,他引:2
生物陶粒柱和粉末活性炭作为淹没式中空纤维膜过滤装置的预处理工艺不仅解决了膜过滤装置氨氮去除不利的弱点,避免了亚硝酸盐氮的积累,而且在浊度、细菌、有机物等方面极大地降低了膜过滤装置的负荷。生物陶粒柱-PAC-膜过滤装置系统高锰酸盐指数平均去除率为76.97%,氨氮和亚硝酸盐氮的平均去除率分别达到顾95.50%和99.15%。 相似文献
3.
分别采用膜生物反应器(MBR)和普通生物反应器(CSTR)对苯胺废水进行处理,结果表明MBR处理效果优于CSTR,处理水苯胺浓度接近动力学极限浓度。测定了两种反应器中微生物的最大比基质利用速率qmax分别为2.084d^-1和1.650d^-1,亲和常数Ks值分别为0.237mg/L和0.309mg/L。间歇试验证明MBR能富集培养基质亲和性高的专一性微生物。这类微生物降解速率不随基质浓度而变化,且能更彻底地降解有机物,适用于微量有机物的高度净化。 相似文献
4.
虾池环境生物修复作用菌的模拟应用 总被引:11,自引:1,他引:11
在模拟条件下,研究了虾池环境生物修复作用菌对对虾养殖环境中虾池有机物的降解过程,结果表明,虾池环境生物修复作用菌能明显改善虾池环境,降低有机物的含量(4d后CODMn的去除率为43.52%)。将大分子的有机物降解为小分子的无机氮等;对虾养殖池中作用菌的使用量以262.5kghm^-2为宜。图3参13 相似文献
5.
针对膜生物反应器(MBR)较长的污泥龄导致磷的处理效果差的问题,采用铁盐强化除磷,向反应器中投加n(Fe)/n(P)=2.0的Fe Cl3·6H2O,系统考察膜生物反应器对氮、有机物及磷的去除效果,重点考察膜生物反应器投加铁盐前后运行性能、活性污泥菌群及膜污染速率变化情况.结果显示,在氮、有机物去除方面,投加前后没有发生明显的变化,去除率始终保持在90%左右.在磷去除方面,投加前磷的平均去除率为52%,投加后去除率提高了近40%,去除效果显著提升.实验进一步研究了加入三价铁盐前后对活性污泥优势菌群和生物除磷的影响.铁盐的投加降低了活性污泥菌群多样性及部分已知聚磷菌的相对丰度,对生物除磷造成一定的负面影响.在膜污染方面,通过跨膜压差(TMP)记录分析此浓度的铁盐并没有导致膜生物反应器膜组件膜污染的加剧.本研究表明,该浓度(n(Fe)/n(P)=2.0)的铁盐进入膜生物反应器会对体系内活性污泥聚磷菌的相对丰度及生物除磷效率造成一定程度上的降低,但对膜污染没有明显影响,可以使出水各项指标尤其是磷的尾水排放浓度达标. 相似文献
6.
改性TiO2光催化膜的制备及其光催化降解2,4-DCP的研究 总被引:6,自引:0,他引:6
利用活性炭粉末对TiO2光催化剂进行改性,并对2,4-二氯苯酚进行光催化降解.结果表明,改性后TiO2光催化剂的光催化活性较之改性前有很大的提高.在pH=10,活性炭粉末掺杂量为10mg·ml-1时,300W高压汞灯下光催化降解120min,2,4DCP的去除率可达96.75%. 相似文献
7.
《应用与环境生物学报》2017,(2)
厌氧膜生物反应器(An MBR)是厌氧生物反应器和膜过滤技术的结合,具有高效降解有机物、能源回收利用等特点,逐渐应用于高浓度有机废水处理领域,但其稳定性较差、膜污染严重等问题制约其工业化应用.本文介绍沸石、活性炭、硬硅钙纤维粒子等不同类型填料投加强化An MBR污染物去除效率、缩短反应器启动时间、提升甲烷产量等的工艺性能研究,分析填料强化工艺电化学作用、吸附作用、强化厌氧污泥颗粒化等的可能机制,指出填料可有效提升工艺性能;综述An MBR工艺膜垢组成及膜污染形成过程,探讨膜材质、操作条件、微生物代谢产物、污泥浓度及菌群结构、废水水质等膜污染的影响因素,在此基础上分析填料投加减缓膜污染机制,以期进一步控制膜污染、延长膜寿命.今后应优选开发经济、高效的新型生物填料及新型组合填料,推广其工业化应用,并从厌氧菌群调控与膜污染控制角度构建高效稳定的An MBR工艺技术体系. 相似文献
8.
固定化生物活性炭处理低浓度甲醇废水 总被引:11,自引:0,他引:11
将分离筛选得到的甲醇降解菌固定在颗粒活性炭上,组成固定化生物活性炭反应系统,研究该反应系统处理轻度污染含甲醇废水的最佳运行条件和运行效果,结果表明,固定化生物活性炭处理轻度污染含甲醇放心水的方法明显好于3种树脂和单纯活性炭吸附处理,反应系统的最佳运行条件是水力负荷0.84-0.77m^3(m^2.h),停留时间57-62min,pH7-8,温度20℃-30℃,溶解氧是去除甲醇的主要限制因子,甲醇含量为11.3-23.1mg/L时,去除率大90%,出水CODcr小于12mg/L。此外还研究了生物活性炭生物膜的一些特点,并分析了运行中活性炭吸附性能的变化。 相似文献
9.
随着水环境外污染源得到有效控制,底质污染逐渐成为人们关注的焦点.底质中的污染物尤其是难降解有机物可通过生物富集和生物放大等过程,进一步影响陆生生物和人类的健康.因此,对底质中难降解有机物的修复是目前所迫切需要解决的环境问题之一.基于异位修复成本较高易造成二次污染等缺点,文章针对难降解有机物污染底质,探讨了原位修复技术的研究进展,自然修复成本较低,对生态环境不产生干扰,但不适用于高浓度污染底质;植物修复操作简单,能有效防止污染底质再悬浮,但对高浓度难降解有机物耐受性较低;微生物修复适用范围广,修复效果较为显著,但菌体易流失,对环境的适应性较差.于是,固定化修复技术应运而生,固定化技术能解决传统的微生物修复存在的很多问题,但固定化载体的重复可利用性和再生性问题仍有待解决.文章最后对今后难降解有机物污染底质的研究方向进行了展望,由于污染底质多为复合污染,各取所长的联合修复技术将成为未来的研究热点. 相似文献
10.
膜分离活性污泥法的研究 总被引:14,自引:0,他引:14
提高生物难降解有机污染物的去除率,改善处理水的水质和达标率,缩小装置的占地面积,节省动力消耗是活性污泥法工艺的发展方向。本试验以膜分离单元代替普通活性污泥法的二沉池,开发了一种新的废水处理工艺。试验结果表明:膜分离活性污泥法对有机物和NH_3-N的去除率比普通活性污泥法高,二级处理可以获得三级处理的效果。根据不同水质和工艺要求,膜孔径应小于20μm,采用水反冲和药液清洗可以确保膜分离装置长期稳定的运行。 相似文献
11.
Xiaoman Liu Chang Tian Yanxia Zhao Weiying Xu Dehua Dong Kaimin Shih Tao Yan Wen Song 《Frontiers of Environmental Science & Engineering》2022,16(8):110
12.
Liu P.Wang Y.Su K. 《应用与环境生物学报》2018,(3):557-562
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. 相似文献
13.
以膜生物反应器(MBR)处理模拟生活废水为研究体系,考察曝气强度对系统污染物去除效果、脱氢酶活性、胞外聚合物(EPS)组分和含量、Zeta电位、污泥粒径及跨膜压差等的影响.结果表明,随着曝气强度降低,COD去除率变化不大,均大于94.0%,脱氢酶活性明显降低,VSS/SS比值下降;污泥LB-EPS增加,Zeta电位降低,污泥平均体积粒径减小,膜通量下降速率增大.曝气强度为800—400 L.m-.2h-1的条件下,曝气产生的水力剪切力不是影响污泥粒径大小的主导因素,污泥Zeta电位则起着决定作用,但水力剪切力有利于缓解膜污染. 相似文献
14.
Cheng Cai Wenjun Sun Siyuan He Yuanna Zhang Xuelin Wang 《Frontiers of Environmental Science & Engineering》2023,17(10):126
15.
Olga S. Arvaniti Marilena E. Dasenaki Alexandros G. Asimakopoulos Niki C. Maragou Vasilios G. Samaras Korina Antoniou Georgia Gatidou Daniel Mamais Constantinos Noutsopoulos Zacharias Frontistis Nikolaos S. Thomaidis Athanasios S. Stasinakis 《Frontiers of Environmental Science & Engineering》2022,16(11):148
16.
Adding iron salt or iron hydroxide to sludgemixed liquor in an aeration tank of a conventional activated sludge processes (bioferric process) can simultaneously improve the sludge’s filterability and enhance the system’s treatment capacity. In view of this, Fe(OH)3 was added to a submerged membrane bioreactor (SMBR) to enhance the removal efficiency and to mitigate membrane fouling. Bioferric process and SMBR were combined to create a novel process called Bioferric-SMBR. A side-by-side comparison study of Bioferric-SMBR and common SMBR dealing with dyeing wastewater was carried out. Bioferric-SMBR showed potential superiority, which could enhance removal efficiency, reduce membrane fouling and improve sludge characteristic. When volumetric loading rate was 25% higher than that of common SMBR, the removal efficiencies of Bioferric-SMBR on COD, dye, and NH4 +-N were 1.0%, 9.5%, and 5.2% higher than that of common SMBR, respectively. The trans-membrane pressure of Bioferric-SMBR was only 36% of that in common SMBR while its membrane flux was 25% higher than that of common SMBR. The stable running period in Bioferric-SMBR was 2.5 times of that in common SMBR when there was no surplus sludge discharged. The mixed liquor suspended solids concentration of Bioferric-SMBR was higher than that of common SMBR with more diversified kinds of microorganisms such as protozoans and metazoans. The mean particle diameter and specific oxygen uptake rate of Bioferric-SMBR were 3.10 and 1.23 times the common SMBR, respectively. 相似文献
17.
Gang Yi Xinfei Fan Xie Quan Shuo Chen Hongtao Yu 《Frontiers of Environmental Science & Engineering》2019,13(2):23
18.
An Ding Yingxue Zhao Zhongsen Yan Langming Bai Haiyang Yang Heng Liang Guibai Li Nanqi Ren 《Frontiers of Environmental Science & Engineering》2020,14(4):59
19.
Chao Pang Chunhua He Zhenhu Hu Shoujun Yuan Wei Wang 《Frontiers of Environmental Science & Engineering》2019,13(4):50
20.
Guangrong Sun Chuanyi Zhang Wei Li Limei Yuan Shilong He Liping Wang 《Frontiers of Environmental Science & Engineering》2019,13(1):1