石家庄经济技术开发区污水处理厂一级A提标改造工艺研究
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摘要
石家庄经济技术开发区污水处理厂设计排放标准为二级标准,根据国家相关法规,必须进行一级A提标改造。该污水处理厂目前接纳的废水90%以上为工业废水,通过传统工艺处理达到一级A排放标准难度较大。本课题拟针对污水的水质特点开展中试研究,确定最佳工艺技术路线,制定一级A提标改造方案,并进行技术及经济可行性分析,为该污水处理厂一级A提标改造工程的实施提供技术支持。
1)建立了一座处理能力为1.0m3/h中试装置,采用"HAF复合厌氧反应池+BFP生物铁反应池+FSBBR流离生物膜反应池+MBBR移动生物膜反应池+臭氧生物炭反应池”工艺,确定各处理单元水利停留时间分别为3.6h、7.8h、5h、7.8h、7.8h和1.5h。试验结果表明,当进水COD300-800mg/L、NH3-N30-60mg/L、TN50-80mg/L、TP5-7mg/L时,COD、NH3-N、TN和TP的去除率分别达到85%、90%、73%和93%以上,出水水质均可满足《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A排放标准,并对各单元运行参数进行优化。
2)在中试研究的基础上,确定了污水处理厂一级A提标改造工艺,并结合污水处理厂‘现有构筑物及厂区平面布置情况,制定了一级A提标改造方案。
3)对一级A提标改造方案的技术及经济可行性分析表明：采取的处理工艺高效、稳定、可靠。改造工程总投资4965.43万元,改造后全厂年运行费用为1234.52万元,吨水运行成本0.748元(不含折旧费和维修费),工程实施后,COD、NH3-N、TN及TP的消减量分别为8213t/a、730t/a、456t/a和63.88t/a,环境社会效益显著。
The effluent designed of the sewage disposal plant of Shijiazhuang economical and technique develop area was secondary standard, according to relevant regulations, the facility must be expanded and upgraded. There are more than 90% of the industrial wastewater in the influents of the plant, which is hard to meet the effluent standard of A in First grade through the traditional wastewater treatment processes. In this paper, a pilot-scale experiment was conducted to determine the optimum technical strategies based on the actual characteristics of the influent, and then made the upgrading reconstruction plan and evaluated the feasibility at technical and economic aspects, aiming at offering a guidance to the upgrading of the operating water plant.
1) A pilot-scale experiment was carried with the process of " HAF+BFP+FSBBR+MBBR+O3/BAC ", the treatment potential was 1.0 m3/h, and the hydraulic retention time were 3.6h,7.8h,5h,7.8h,7.8h and 1.5h, respectively. The research indicated that:when the quality of influents was COD 300-800mg/L, NH3-N 30-60mg/L, TN 50-80mg/L and TP 5-7mg/L, the removal efficiency of COD, NH3-N, TN and TP were more than 85%,90%,73% and 93%, respectively. Each index of effluent reached the primary standard level A of discharge standard of pollutants for municipal wastewater treatment plant (GB18918-2002), and then operating parameters of each unit were optimized.
2) The upgrading reconstruction plan were drafted combining the main structures and plane arrangement of the sewage treatment plant and the design process of sewage treatment plan which was made on the basis of pilot-scale experiment.
3) The economic and technical feasibility study of the upgrading reconstruction plan indicated that the process is efficient, stable and reliable. The total investment of reconstruction project was 4965.43×104 yuan, the annual operating cost of the whole plant was 1234.52×104yuan, and the running cost was only 0.748 yuan/t. This project was estimated to reduce the emissions of COD, NH3-N, TN, TP about 8213t/a,730t/a,456t/a, 63.88t/a, respectively and the social benefits and environmental benefits of the project were incalculable.
1)建立了一座处理能力为1.0m3/h中试装置,采用"HAF复合厌氧反应池+BFP生物铁反应池+FSBBR流离生物膜反应池+MBBR移动生物膜反应池+臭氧生物炭反应池”工艺,确定各处理单元水利停留时间分别为3.6h、7.8h、5h、7.8h、7.8h和1.5h。试验结果表明,当进水COD300-800mg/L、NH3-N30-60mg/L、TN50-80mg/L、TP5-7mg/L时,COD、NH3-N、TN和TP的去除率分别达到85%、90%、73%和93%以上,出水水质均可满足《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A排放标准,并对各单元运行参数进行优化。
2)在中试研究的基础上,确定了污水处理厂一级A提标改造工艺,并结合污水处理厂‘现有构筑物及厂区平面布置情况,制定了一级A提标改造方案。
3)对一级A提标改造方案的技术及经济可行性分析表明：采取的处理工艺高效、稳定、可靠。改造工程总投资4965.43万元,改造后全厂年运行费用为1234.52万元,吨水运行成本0.748元(不含折旧费和维修费),工程实施后,COD、NH3-N、TN及TP的消减量分别为8213t/a、730t/a、456t/a和63.88t/a,环境社会效益显著。
The effluent designed of the sewage disposal plant of Shijiazhuang economical and technique develop area was secondary standard, according to relevant regulations, the facility must be expanded and upgraded. There are more than 90% of the industrial wastewater in the influents of the plant, which is hard to meet the effluent standard of A in First grade through the traditional wastewater treatment processes. In this paper, a pilot-scale experiment was conducted to determine the optimum technical strategies based on the actual characteristics of the influent, and then made the upgrading reconstruction plan and evaluated the feasibility at technical and economic aspects, aiming at offering a guidance to the upgrading of the operating water plant.
1) A pilot-scale experiment was carried with the process of " HAF+BFP+FSBBR+MBBR+O3/BAC ", the treatment potential was 1.0 m3/h, and the hydraulic retention time were 3.6h,7.8h,5h,7.8h,7.8h and 1.5h, respectively. The research indicated that:when the quality of influents was COD 300-800mg/L, NH3-N 30-60mg/L, TN 50-80mg/L and TP 5-7mg/L, the removal efficiency of COD, NH3-N, TN and TP were more than 85%,90%,73% and 93%, respectively. Each index of effluent reached the primary standard level A of discharge standard of pollutants for municipal wastewater treatment plant (GB18918-2002), and then operating parameters of each unit were optimized.
2) The upgrading reconstruction plan were drafted combining the main structures and plane arrangement of the sewage treatment plant and the design process of sewage treatment plan which was made on the basis of pilot-scale experiment.
3) The economic and technical feasibility study of the upgrading reconstruction plan indicated that the process is efficient, stable and reliable. The total investment of reconstruction project was 4965.43×104 yuan, the annual operating cost of the whole plant was 1234.52×104yuan, and the running cost was only 0.748 yuan/t. This project was estimated to reduce the emissions of COD, NH3-N, TN, TP about 8213t/a,730t/a,456t/a, 63.88t/a, respectively and the social benefits and environmental benefits of the project were incalculable.
引文
[1]黄克亮.城市污水生物处理工艺研究.科技信息,2010,(34)：341
[2]王宝贞,沈耀良.废水生物处理新技术理论与应用.北京：中国环境科学出版社,2006：1-45
[3]徐春来,马寅初.AB工艺在生活污水处理中的应用.科技情报开发与经济,2007,17(23)：279-280
[4]杜红,邹利安,王宝贞.深圳市罗芳污水处理厂AB工艺的运行控制与维护管理.给水排水,2004,30(10)：13-16
[5]海里且木·买买提,迪丽努尔·塔力甫.鸟鲁木齐市河东污水J AB法处理污水过程的评价.环境工程,2005,23(3)：56-57
[6]X. H.WANG, K. ZHANG, N. Q. REN. Monitoring microbial community structure and succession of an A/O SBR during start-up period using PCR-DGGE. Journal of Environmental Sciences,2009, (2):223-228
[7]王晨.曝气生物滤池工艺的工程应用研究.[上海交通大学硕士论文].2008：1-13
[8]黄赞洲,陈宗庆.A/O工艺在中小型生活污水处理站的应用.广两轻工业,2009,25(7)：95-96
[9]G. B. ZHU, Y. Z. PENG, S. Y. WANG, et al. Comparative study of two biological nitrogen removal processes:A/O process and step-feeding process. Journal of Southeast University,2008, 24 (4):528-531
[10]袁丁,柯鹏,刘义清.A2/O与氧化沟一体化工艺在污水处理厂中的应用.化学工程师,2008,22(7)：50-51,67-68
[11]唐翀鹏,冯健,王水.A2/O工艺在邳州城北污水处理厂的应用.环境科技,2010,23(3)：40-45
[12]侯金良,康勇.城市污水生物脱氧除磷技术的研究进展.化工进展,2007,26(3)：366-376
[13]王莉.改良型A2/O工艺脱氧除磷效果的分析.江两化工,2007,(4)：122-124
[14]R. BLACKBURNE, Z. YUAN, J. KELLER. Demonstration of nitrogen removal via nitrite in a sequencing batch reactor treating domestic wastewater. Water Research,2008,42(8-9):2166-2176
[15]C. S. RA, K. V. LO, J. S. SHIN, et al. Biological Nutrient Removal with an Internal Organic Carbon Source in piggery wastewater treatment. Water Research,2000,34(3):965-97
[16]A. CARUCCI, A. CHIAVOLA, M. MAJONE, et al. Treatment of tannery wastewater in sequencing batch reactor. Water Science Technology,1999,40(1):253-259
[17]M. KABAINSKI, B. HULTMAN, E. PLAZA, et al. Strategies for improvement of sludge quality and process performance of sequencing batch reator plant treating municipal and tannery wastewater. Water Science Technology,1998,38(4-5):69-77
[18]何景苹,李闫.浅谈城市污水处理厂的设计工艺.黑龙江科技信息,2010,(6)：66
[19]李建平.循环式SBR处理城市污水工程实例.河南城建学院学报,2010,19(6)：33-35
[20]Y. C. LIU. Study of operational conditions of simultaneous nitrification and denitrification in a Carrousel oxidation ditch for domestic wastewater treatment. Bioresource Technology,2010,101 (3):901-906
[21]任红娟.我国城市污水处理的主要工艺及发展趋势.中国建设教育,2004,4(4)：58-60
[22]王宇.城市污水处理厂工艺类型与优化选择研究.河南化工,2010,27(4)：36-37
[23]龙莹.小型城市污水处理工艺方案的选择.广西工学院学报,2006,(1)：32-36
[24]王淑贤.小城镇污水处理工艺流程的选择.绿色科技,2011,(2)：87-89
[25]H. ODEGAARD, B. RUSTEN, T. WESTRUN. A new moving bed biofilm reactor application and results. Water Science and Technology,1994,29 (10):157-165
[26]王奕,张兴义,杨凤林.移动床生物膜反应器的研究及应用现状.环境治理技术与设备,2002,3(7)：78-80
[27]廖榆敏,汤兵,陈秋雯.移动床生物反应器启动特性研究进展.水处理技术,2011,37(2)：5-8
[28]M. RODGERS, X. M. ZHAN. Moving-medium biofilm reactors. Environmental Science and Biotechnology,2007, (2):213-224
[29]B. RUSTEN, B. EIKEBROK, Y. ULGENES. Design and operations of the kaldnes moving bed biofilm reactors. Aquacultural Engineering,2006,322-331
[30]G. Pastorelli, G. Andreottola, R. Canziani, et al. Pilot-plant experiments with moving-bed biofilm reactors. Water Science and Technology,1997,36(1):43-50
[31]M. RODGERS, X. M. ZHAN, B. GALLAGHER. A pilot plant study using a vertically moving biofilm process to treat municipal wastewater. Bioresource Technology,2003,89 (2):139-143
[32]赵勇,任玉斌.悬浮填料处理市政废水的实验研究.污染防治技术,2008,21(2)：15-17
[33]陈轶波,夏四清,吴育文.悬浮填料床处理城市污水的中试研究.中国资源综合利用,2008,26(8)：6-8
[34]刘黎慧,杨应桥,周朝听,等.移动床生物膜反应器处理生活污水的研究.市政技术,2009,27(2)：161-164
[35]魏海娟,张水祥,张粲.序批式MBBR处理低C/N生活污水.工业水处理,2009,29(3)：46-49
[36]马亚钦,苗利峰,姚亮.移动床生物膜反应器工艺在污水处理厂改造中的应用.清洗世界,2008,24(9)：6-9
[37]饶雪峰,邢奕,邹安华MBBR处理三河市城市污水的工程应用.给水排水,2006,32(10)： 25-27
[38]李占臣,唐超,吕树芳.MBR处理城市生活污水的研究.环境科技,2010,23(1)：31-33
[39]S. H. KIM, S. Y. MOON, C. H. YOON, et al. Role of coagulation in membrane filtration of wastewater for reuse. Desalination,2005, (173):301-307
[40]杨开基.MBR在污水处理中的应用研究.科技情报开发与经济,2010,20(24)：151-152
[41]胡邦,蒋岚岚,张万里,等.MBR工艺在城市污水处理厂中的工程应用.给水排水,2009,35(11)：23-24
[42]高延耀,顾国维,周琪.水污染控制工程(第三版).北京：高等教育出版社,2008,150
[43]宋安宁,娄性义,韩片：.新西兰罗托鲁阿污水处理厂的处理工艺.中国环保产业,2005(2)：42-43
[44]吴涛.混凝-超滤T艺处理城市二级出水回用于景观水体的研究.[长安大学硕士论文].2006：2-18
[45]M. AGOPSOWICZ, A. BIALOWIEC, P. PIJARCZYK. Sewage sludge land disposal effects on groundwater. Archives of environmental protection,2008,34(2):73-82
[46]王允妹.城市污水二级处理出水用于地下回灌的深度处理技术研究.环境保护科学,2008,34(1)：27-29
[47]陈越,李玉华.BAF-混凝-沉淀-过滤工艺在中水回用中的应用.给水排水,2007,(33)：33-35
[48]陈广银,陈洪斌,何群彪,等CEPT-曝气生物滤池低温下处理模拟废水的应用研究.环境T程学报,2009.3(6)：1007-1010
[49]D. W. HAN, H. J. YUN, D. J. KIM. Autotrophic nitrification and denitrification characteristics of an up flow biological aerated filter. Journal of chemical Technology and Biotechnology,2001, 76(11):1112-1116
[50]H. D. RYU, D. KIM, H. E. LIM, et al. Development and application of kinetic model on biological anoxic/aeroic filter. Chemosphere,2008,70(6):990-1001
[51]E. ROTHER, P. CORNEL, A. ANTE, et al. Comparison of combined and separated biological aerated filter (BAF) Performance for Predenitrification/nitrification of municipal wastewater. Water Science and Technology,2002,46(4):149-158
[52]郭锋,王潇,肖强,等.臭氧生物活性炭技术在水处理中的应用与研究.工业水处理,2011,31(3)：19-23
[53]刘通,孙贤波,刘勇弟.活性炭吸附对生化出水中不同种类有机物的去除效果.环境化学,2009,28(3)：369-372
[54]陈浩玺,贾振民.生物炭-臭氧技术在中水处理中的应用.工业水处理,2006,26(1)：76-78
[55]李琳琳,单学敏,高丽.超滤技术在水处理中的应用研究.安全与环境工程,2010,17(6)： 5-8
[56]G. Crozes. Effect of adsorption of organic matter on fouling of UF membrane. Membrane Science,2003,94(10):61-77
[57]A. M. RAVAZZINI, A. F. VAN NIEUWENHUIJZENA, J. H. M. J. VAN DER GRAAFA. Direct ultra-filtration of municipal wastewater:comparison between filtration of raw sewage and primary clarifier effluent. Desalination,2005,178(1-3):51-62
[58]C. W. LEE, S. D. BAE, S. W. HAN, et al. Application of ultra-filtration hybrid membrane processes for reuse of secondary effluent. Desalination,2007, (202):239-246
[59]杨琦,尚海涛,席宏波,等.超滤反渗透处理城市二级生活污水处理厂出水中试研究.膜科学与技术,2007,27(3)：71-74
[60]蔡正文.生化处理工艺对有毒难降解化工废水处理的实验研究.四川化工,2010,13(3)：50-53
[61]汤贵兰,蓝伟光,张烨,等.焦炭和废铁屑微电解预处理垃圾渗滤液的研究.环境污染治理技术与设备,2006,7(1])：121-123
[62]邱珉,徐晓军.铁碳微电解法在废水处理中的研究应用进展.两南给排水,2009,31(4)：21-24
[63]朱泉支.铁碳微电解法在废水预处理过程中的应用现状及前景.科技资讯,2011,(2)：118
[64]王泞,沈雁群,高冲,等. MBBR同步硝化反硝化生物脱氮技术研究进展.湖北民族学院学报,2011,29(1)：8-12
[65]王立立,胡勇有.BAF与MBBR工艺在小区生活污水处理中的应用对比.安全与环境学报,2008,8(5)：26-31
[66]李碧MBBR工艺的研究现状与应用.中国环保产业,2009,(1)：20-23
[67]黄小华.浅谈城废市污水处理中的脱氮除磷方法.中国科技信息,2009,(13)：24-25
[2]王宝贞,沈耀良.废水生物处理新技术理论与应用.北京：中国环境科学出版社,2006：1-45
[3]徐春来,马寅初.AB工艺在生活污水处理中的应用.科技情报开发与经济,2007,17(23)：279-280
[4]杜红,邹利安,王宝贞.深圳市罗芳污水处理厂AB工艺的运行控制与维护管理.给水排水,2004,30(10)：13-16
[5]海里且木·买买提,迪丽努尔·塔力甫.鸟鲁木齐市河东污水J AB法处理污水过程的评价.环境工程,2005,23(3)：56-57
[6]X. H.WANG, K. ZHANG, N. Q. REN. Monitoring microbial community structure and succession of an A/O SBR during start-up period using PCR-DGGE. Journal of Environmental Sciences,2009, (2):223-228
[7]王晨.曝气生物滤池工艺的工程应用研究.[上海交通大学硕士论文].2008：1-13
[8]黄赞洲,陈宗庆.A/O工艺在中小型生活污水处理站的应用.广两轻工业,2009,25(7)：95-96
[9]G. B. ZHU, Y. Z. PENG, S. Y. WANG, et al. Comparative study of two biological nitrogen removal processes:A/O process and step-feeding process. Journal of Southeast University,2008, 24 (4):528-531
[10]袁丁,柯鹏,刘义清.A2/O与氧化沟一体化工艺在污水处理厂中的应用.化学工程师,2008,22(7)：50-51,67-68
[11]唐翀鹏,冯健,王水.A2/O工艺在邳州城北污水处理厂的应用.环境科技,2010,23(3)：40-45
[12]侯金良,康勇.城市污水生物脱氧除磷技术的研究进展.化工进展,2007,26(3)：366-376
[13]王莉.改良型A2/O工艺脱氧除磷效果的分析.江两化工,2007,(4)：122-124
[14]R. BLACKBURNE, Z. YUAN, J. KELLER. Demonstration of nitrogen removal via nitrite in a sequencing batch reactor treating domestic wastewater. Water Research,2008,42(8-9):2166-2176
[15]C. S. RA, K. V. LO, J. S. SHIN, et al. Biological Nutrient Removal with an Internal Organic Carbon Source in piggery wastewater treatment. Water Research,2000,34(3):965-97
[16]A. CARUCCI, A. CHIAVOLA, M. MAJONE, et al. Treatment of tannery wastewater in sequencing batch reactor. Water Science Technology,1999,40(1):253-259
[17]M. KABAINSKI, B. HULTMAN, E. PLAZA, et al. Strategies for improvement of sludge quality and process performance of sequencing batch reator plant treating municipal and tannery wastewater. Water Science Technology,1998,38(4-5):69-77
[18]何景苹,李闫.浅谈城市污水处理厂的设计工艺.黑龙江科技信息,2010,(6)：66
[19]李建平.循环式SBR处理城市污水工程实例.河南城建学院学报,2010,19(6)：33-35
[20]Y. C. LIU. Study of operational conditions of simultaneous nitrification and denitrification in a Carrousel oxidation ditch for domestic wastewater treatment. Bioresource Technology,2010,101 (3):901-906
[21]任红娟.我国城市污水处理的主要工艺及发展趋势.中国建设教育,2004,4(4)：58-60
[22]王宇.城市污水处理厂工艺类型与优化选择研究.河南化工,2010,27(4)：36-37
[23]龙莹.小型城市污水处理工艺方案的选择.广西工学院学报,2006,(1)：32-36
[24]王淑贤.小城镇污水处理工艺流程的选择.绿色科技,2011,(2)：87-89
[25]H. ODEGAARD, B. RUSTEN, T. WESTRUN. A new moving bed biofilm reactor application and results. Water Science and Technology,1994,29 (10):157-165
[26]王奕,张兴义,杨凤林.移动床生物膜反应器的研究及应用现状.环境治理技术与设备,2002,3(7)：78-80
[27]廖榆敏,汤兵,陈秋雯.移动床生物反应器启动特性研究进展.水处理技术,2011,37(2)：5-8
[28]M. RODGERS, X. M. ZHAN. Moving-medium biofilm reactors. Environmental Science and Biotechnology,2007, (2):213-224
[29]B. RUSTEN, B. EIKEBROK, Y. ULGENES. Design and operations of the kaldnes moving bed biofilm reactors. Aquacultural Engineering,2006,322-331
[30]G. Pastorelli, G. Andreottola, R. Canziani, et al. Pilot-plant experiments with moving-bed biofilm reactors. Water Science and Technology,1997,36(1):43-50
[31]M. RODGERS, X. M. ZHAN, B. GALLAGHER. A pilot plant study using a vertically moving biofilm process to treat municipal wastewater. Bioresource Technology,2003,89 (2):139-143
[32]赵勇,任玉斌.悬浮填料处理市政废水的实验研究.污染防治技术,2008,21(2)：15-17
[33]陈轶波,夏四清,吴育文.悬浮填料床处理城市污水的中试研究.中国资源综合利用,2008,26(8)：6-8
[34]刘黎慧,杨应桥,周朝听,等.移动床生物膜反应器处理生活污水的研究.市政技术,2009,27(2)：161-164
[35]魏海娟,张水祥,张粲.序批式MBBR处理低C/N生活污水.工业水处理,2009,29(3)：46-49
[36]马亚钦,苗利峰,姚亮.移动床生物膜反应器工艺在污水处理厂改造中的应用.清洗世界,2008,24(9)：6-9
[37]饶雪峰,邢奕,邹安华MBBR处理三河市城市污水的工程应用.给水排水,2006,32(10)： 25-27
[38]李占臣,唐超,吕树芳.MBR处理城市生活污水的研究.环境科技,2010,23(1)：31-33
[39]S. H. KIM, S. Y. MOON, C. H. YOON, et al. Role of coagulation in membrane filtration of wastewater for reuse. Desalination,2005, (173):301-307
[40]杨开基.MBR在污水处理中的应用研究.科技情报开发与经济,2010,20(24)：151-152
[41]胡邦,蒋岚岚,张万里,等.MBR工艺在城市污水处理厂中的工程应用.给水排水,2009,35(11)：23-24
[42]高延耀,顾国维,周琪.水污染控制工程(第三版).北京：高等教育出版社,2008,150
[43]宋安宁,娄性义,韩片：.新西兰罗托鲁阿污水处理厂的处理工艺.中国环保产业,2005(2)：42-43
[44]吴涛.混凝-超滤T艺处理城市二级出水回用于景观水体的研究.[长安大学硕士论文].2006：2-18
[45]M. AGOPSOWICZ, A. BIALOWIEC, P. PIJARCZYK. Sewage sludge land disposal effects on groundwater. Archives of environmental protection,2008,34(2):73-82
[46]王允妹.城市污水二级处理出水用于地下回灌的深度处理技术研究.环境保护科学,2008,34(1)：27-29
[47]陈越,李玉华.BAF-混凝-沉淀-过滤工艺在中水回用中的应用.给水排水,2007,(33)：33-35
[48]陈广银,陈洪斌,何群彪,等CEPT-曝气生物滤池低温下处理模拟废水的应用研究.环境T程学报,2009.3(6)：1007-1010
[49]D. W. HAN, H. J. YUN, D. J. KIM. Autotrophic nitrification and denitrification characteristics of an up flow biological aerated filter. Journal of chemical Technology and Biotechnology,2001, 76(11):1112-1116
[50]H. D. RYU, D. KIM, H. E. LIM, et al. Development and application of kinetic model on biological anoxic/aeroic filter. Chemosphere,2008,70(6):990-1001
[51]E. ROTHER, P. CORNEL, A. ANTE, et al. Comparison of combined and separated biological aerated filter (BAF) Performance for Predenitrification/nitrification of municipal wastewater. Water Science and Technology,2002,46(4):149-158
[52]郭锋,王潇,肖强,等.臭氧生物活性炭技术在水处理中的应用与研究.工业水处理,2011,31(3)：19-23
[53]刘通,孙贤波,刘勇弟.活性炭吸附对生化出水中不同种类有机物的去除效果.环境化学,2009,28(3)：369-372
[54]陈浩玺,贾振民.生物炭-臭氧技术在中水处理中的应用.工业水处理,2006,26(1)：76-78
[55]李琳琳,单学敏,高丽.超滤技术在水处理中的应用研究.安全与环境工程,2010,17(6)： 5-8
[56]G. Crozes. Effect of adsorption of organic matter on fouling of UF membrane. Membrane Science,2003,94(10):61-77
[57]A. M. RAVAZZINI, A. F. VAN NIEUWENHUIJZENA, J. H. M. J. VAN DER GRAAFA. Direct ultra-filtration of municipal wastewater:comparison between filtration of raw sewage and primary clarifier effluent. Desalination,2005,178(1-3):51-62
[58]C. W. LEE, S. D. BAE, S. W. HAN, et al. Application of ultra-filtration hybrid membrane processes for reuse of secondary effluent. Desalination,2007, (202):239-246
[59]杨琦,尚海涛,席宏波,等.超滤反渗透处理城市二级生活污水处理厂出水中试研究.膜科学与技术,2007,27(3)：71-74
[60]蔡正文.生化处理工艺对有毒难降解化工废水处理的实验研究.四川化工,2010,13(3)：50-53
[61]汤贵兰,蓝伟光,张烨,等.焦炭和废铁屑微电解预处理垃圾渗滤液的研究.环境污染治理技术与设备,2006,7(1])：121-123
[62]邱珉,徐晓军.铁碳微电解法在废水处理中的研究应用进展.两南给排水,2009,31(4)：21-24
[63]朱泉支.铁碳微电解法在废水预处理过程中的应用现状及前景.科技资讯,2011,(2)：118
[64]王泞,沈雁群,高冲,等. MBBR同步硝化反硝化生物脱氮技术研究进展.湖北民族学院学报,2011,29(1)：8-12
[65]王立立,胡勇有.BAF与MBBR工艺在小区生活污水处理中的应用对比.安全与环境学报,2008,8(5)：26-31
[66]李碧MBBR工艺的研究现状与应用.中国环保产业,2009,(1)：20-23
[67]黄小华.浅谈城废市污水处理中的脱氮除磷方法.中国科技信息,2009,(13)：24-25