欢迎登录材料期刊网

材料期刊网

高级检索

本文针对了膜生物反应器(membrane bioreactor,MBR)污泥混合液在铁钙离子共存情况下对MBR运行的影响进行研究.实验结果表明:不同比例的铁钙离子共存时,COD、NH3-N、TP的去除率分别高达94%、98%、98%以上;进一步研究发现,对于调控MBR混合液存在最佳的铁钙离子比,当铁钙离子比为1∶3时,最大程度延缓了膜污染速率;钙离子的加入,MBR混合液中溶解性微生物产物(soluble microbial products,SMP)浓度降低明显,其中SMP中多聚糖含量与钙离子浓度密切相关;在铁钙离子共存体系,钙离子含量对松散结合态EPS(loosely bound EPS,LB)浓度影响较大,对紧密结合态EPS(tightly bound,TB)影响不显著.

参考文献

[1] Hongjun Lin;Weijue Gao;Fangang Meng;Bao-Qiang Liao;Kam-Tin Leung;Leihong Zhaoe;Jianrong Chen;Huachang Hong .Membrane Bioreactors for Industrial Wastewater Treatment: A Critical Review[J].Critical reviews in environmental science and technology,2012(5/8):677-740.
[2] Hong, H.;Peng, W.;Zhang, M.;Chen, J.;He, Y.;Wang, F.;Weng, X.;Yu, H.;Lin, H..Thermodynamic analysis of membrane fouling in a submerged membrane bioreactor and its implications[J].Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies,2013:7-14.
[3] Lin, H.;Liao, B.-Q.;Chen, J.;Gao, W.;Wang, L.;Wang, F.;Lu, X. .New insights into membrane fouling in a submerged anaerobic membrane bioreactor based on characterization of cake sludge and bulk sludge[J].Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies,2011(3):2373-2379.
[4] R. Van den Broeck;J. Van Dierdonck;B. Caerts .The impact of deflocculation-reflocculation on fouling in membrane bioreactors[J].Separation and Purification Technology,2010(3):279-284.
[5] Daivd C. Sobeck;Matthew J. Higgins .Examination of three theories for mechanisms of cation-induced bioflocculation[J].Water research: A journal of the international water association,2002(3):527-538.
[6] Mehrnia, M.R.;Azami, H.;Sarrafzadeh, M.H..Fouling mitigation in membrane bioreactors using multivalent cations[J].Colloids and Surfaces, B. Biointerfaces,2013:90-96.
[7] Jinling Wu;Xia Huang .Effect of dosing polymeric ferric sulfate on fouling characteristics, mixed liquor properties and performance in a long-term running membrane bioreactor[J].Separation and Purification Technology,2008(1):45-52.
[8] Kang Chen;Xinhua Wang;Xiufen Li.Impacts of sludge retention time on the performance of submerged membrane bioreactor with the addition of calcium ion[J].Separation and Purification Technology,2011:148-155.
[9] Rupak Aryal;Julie Lebegue;Saravamuthu Vigneswaran .Identification and characterisation of biofilm formed on membrane bio-reactor[J].Separation and Purification Technology,2009(1):86-94.
[10] 张海丰,刘洪鹏,赵贵龙,张德义.MBR 中微生物代谢产物对膜污染的影响及其调控方法的研究进展[J].东北电力大学学报,2013(04):2-7.
[11] ZHANG Hai-feng,孙宝盛,ZHAO Xin-hua,齐庚申,XU Yan-hong.三氯化铁混凝作用提高膜生物反应器混合液可滤性[J].天津大学学报,2008(02):131-136.
[12] 程汉林.生物铁法和生物铁填料法在难降解有机废水处理中的应用[J].环境技术,2004(03):30-31,33.
[13] Li, H.;Wen, Y.;Cao, A.;Huang, J.;Zhou, Q.;Somasundaran, P. .The influence of additives (Ca ~(2+), Al ~(3+), and Fe ~(3+)) on the interaction energy and loosely bound extracellular polymeric substances (EPS) of activated sludge and their flocculation mechanisms[J].Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies,2012(1):188-194.
[14] ZHANG Hanmin;XIA Jie;YANG Yang;WANG Zixing;YANG Fenglin .Mechanism of calcium mitigating membrane fouling in submerged membrane bioreactors[J].Journal of environmental sciences,2009(8):1066-1073.
[15] Le-Clech P;Chen V;Fane TAG .Fouling in membrane bioreactors used in wastewater treatment[J].Journal of Membrane Science,2006(1/2):17-53.
[16] In S. Kim;Namjung Jang .The effect of calcium on the membrane biofouling in the membrane bioreactor (MBR)[J].Water research: A journal of the international water association,2006(14):2756-2764.
[17] 郗丽娟,吕娜,张海丰,孙宝盛.SMP形成与降解机制分析及其对MBR膜过滤的影响[J].化工学报,2013(08):3003-3008.
[18] Sheng GP;Yu HQ;Li XY .Extracellular polymeric substances (EPS) of microbial aggregates in biological wastewater treatment systems: a review. [Review][J].Biotechnology Advances: An International Review Journal,2010(6):882-894.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%