SBR工艺在污水处理工程中的应用研究
摘要
近几年来,随着我国经济的迅猛发展,对环境所造成的污染也不断加剧。因此,有必要采取有效的措施对废水进行处理,保护生态环境和人类健康。
本研究课题较全面的介绍了天津蓟县经济开发区污水处理厂——本课题依托工程,较深入的研究了SBR工艺处理废水过程中有机底物的降解规律。通过对该污水处理厂的运行效率、工艺机理、影响因素等的分析,证明该方案具有工艺先进、技术可行、经济合理等优点,出水水质稳定且能达到《城镇污水处理厂污染物排放标准》(GB18918-2002)的二级排放标准。
以格栅、曝气沉砂池和气浮池作为整个废水处理流程的预处理单元,目的在于去除废水中较大的砂子、悬浮物和动植物油。
SBR作为核心处理单元,依靠系统内活性污泥的吸附和代谢作用进一步去除废水中的有机负荷及前处理单元中残余的胶体和悬浮物质。本课题从SBR生化系统的启动到正常运行,对系统内微生物的种类与活性、系统的环境(pH、DO、温度、营养物等)等因素进行了研究。对调试和运行中出现的问题进行了重点研究,采取了一定的措施加快了活性污泥的培养与驯化,根据实际情况合理调整SBR池的运行工况,经过一个多月的调试,系统转入了正常运行。
根据Monod方程进行了SBR工艺处理废水的动力学分析,建立并推导了适用于该工艺基质降解的数学模型,验证了SBR反应器中CODCr的降解过程较好地服从一级反应动力学关系式,并得到了适于该水质的动力学参数,从而定量地描述了有机底物降解规律及活性污泥增长规律。
该工艺实际运行和技术经济分析结果表明,其处理效果较好、运行稳定、抗冲击负荷能力强,基建投资和运行费用相对都较低,与同类废水其它生化法处理工艺比较,具有较大的优势。该工艺固定资产投资为700万元,实际运行费用仅为0.62元/m3,是一种技术可行、经济合理的废水处理方法。
In recent years, environment pollution is becoming more serious with the economic development .So it is necessary to take effective measures to treat the wastewater and protect the ecosystem environment and human health.
In this paper, the wastewater treatment plant of Jixian economic technology development zone in Tianjin——the engineering this thesis concerns is presented comprehensively. Degradation law of organic substance in the treatment process of wastewater by sequencing batch reactor is studied deeply. The analysis about waste- water treatment plant on operation efficiency, reaction mechanism and influence factors indicate that this process is advanced, economical and feasible. The effluent is stable and can meet the Discharge Standard of pollutants for municipal wastewater treatment plant of GB18918-2002.
The grille, aeration settlement tank and air-striping tank are used as pretreatment unit in all process, aiming to remove sand , suspended material and animal-plant oil.
As a key unit ,SBR can further eliminate the organic load of the wastewater and also the colloid and suspend substance through the adsorption and metabolism of the active sludge. From the start to the normal operation of the SBR system, this paper researches the species and activity of the microbios in the system. At meantime, the factors , such as pH, DO, temperature, and nutrition etc., are researched too. The problems arising in the preliminary testing and run are researched , and some measures are also taken to speed up the cultivation of active sludge and adjust the operating mode according to the real condition. After the operation of more than a month , the system runs normally.
Kinetic analysis of industrial wastewater by sequencing batch reactor is developed on the basis of Monod model. The mathematic model of SBR treatment system strictly obeys the first-order kinetics relation under the condition of experimental concentration. Experimental results are consistent with the model and kinetic parameters fitting for the water quality were obtained. Therefore, regulations of organic substance degradation and activated sludge growth become available.
The wonderful effect of treatment, stable run ,strong resistant to organic load and the low of capital construction and the cost of run show that the process has an advantage over other process viewing from the run and economical analysis. The fixed property cost of the process is 7,000,000 yuan and the operation cost is 0.62 yuan /m3. All of these show that the SBR process is a suitable way to treat the wastewater, both in the point of feasibility of technology and economical.
本研究课题较全面的介绍了天津蓟县经济开发区污水处理厂——本课题依托工程,较深入的研究了SBR工艺处理废水过程中有机底物的降解规律。通过对该污水处理厂的运行效率、工艺机理、影响因素等的分析,证明该方案具有工艺先进、技术可行、经济合理等优点,出水水质稳定且能达到《城镇污水处理厂污染物排放标准》(GB18918-2002)的二级排放标准。
以格栅、曝气沉砂池和气浮池作为整个废水处理流程的预处理单元,目的在于去除废水中较大的砂子、悬浮物和动植物油。
SBR作为核心处理单元,依靠系统内活性污泥的吸附和代谢作用进一步去除废水中的有机负荷及前处理单元中残余的胶体和悬浮物质。本课题从SBR生化系统的启动到正常运行,对系统内微生物的种类与活性、系统的环境(pH、DO、温度、营养物等)等因素进行了研究。对调试和运行中出现的问题进行了重点研究,采取了一定的措施加快了活性污泥的培养与驯化,根据实际情况合理调整SBR池的运行工况,经过一个多月的调试,系统转入了正常运行。
根据Monod方程进行了SBR工艺处理废水的动力学分析,建立并推导了适用于该工艺基质降解的数学模型,验证了SBR反应器中CODCr的降解过程较好地服从一级反应动力学关系式,并得到了适于该水质的动力学参数,从而定量地描述了有机底物降解规律及活性污泥增长规律。
该工艺实际运行和技术经济分析结果表明,其处理效果较好、运行稳定、抗冲击负荷能力强,基建投资和运行费用相对都较低,与同类废水其它生化法处理工艺比较,具有较大的优势。该工艺固定资产投资为700万元,实际运行费用仅为0.62元/m3,是一种技术可行、经济合理的废水处理方法。
In recent years, environment pollution is becoming more serious with the economic development .So it is necessary to take effective measures to treat the wastewater and protect the ecosystem environment and human health.
In this paper, the wastewater treatment plant of Jixian economic technology development zone in Tianjin——the engineering this thesis concerns is presented comprehensively. Degradation law of organic substance in the treatment process of wastewater by sequencing batch reactor is studied deeply. The analysis about waste- water treatment plant on operation efficiency, reaction mechanism and influence factors indicate that this process is advanced, economical and feasible. The effluent is stable and can meet the Discharge Standard of pollutants for municipal wastewater treatment plant of GB18918-2002.
The grille, aeration settlement tank and air-striping tank are used as pretreatment unit in all process, aiming to remove sand , suspended material and animal-plant oil.
As a key unit ,SBR can further eliminate the organic load of the wastewater and also the colloid and suspend substance through the adsorption and metabolism of the active sludge. From the start to the normal operation of the SBR system, this paper researches the species and activity of the microbios in the system. At meantime, the factors , such as pH, DO, temperature, and nutrition etc., are researched too. The problems arising in the preliminary testing and run are researched , and some measures are also taken to speed up the cultivation of active sludge and adjust the operating mode according to the real condition. After the operation of more than a month , the system runs normally.
Kinetic analysis of industrial wastewater by sequencing batch reactor is developed on the basis of Monod model. The mathematic model of SBR treatment system strictly obeys the first-order kinetics relation under the condition of experimental concentration. Experimental results are consistent with the model and kinetic parameters fitting for the water quality were obtained. Therefore, regulations of organic substance degradation and activated sludge growth become available.
The wonderful effect of treatment, stable run ,strong resistant to organic load and the low of capital construction and the cost of run show that the process has an advantage over other process viewing from the run and economical analysis. The fixed property cost of the process is 7,000,000 yuan and the operation cost is 0.62 yuan /m3. All of these show that the SBR process is a suitable way to treat the wastewater, both in the point of feasibility of technology and economical.
引文
[1]北京市环境保护科学研究院等主编.三废处理工程技术手册:废水卷[M].北京:化学工业出版社,2000
[2]顾国维.水污染治理技术研究[M].上海:同济大学出版社,1997
[3]张自杰.排水工程(下)[M].北京:中国建筑工业出版社,1996
[4]赵丽珍,缪应棋.SBR技术的研究及进展[J].江苏理工大学学报,2001, 1(5):32-35
[5]沈耀良,王宝贞.废水生物处理新技术——理论与应用[M].北京:中国环境科学出版社,2001
[6]于彩霞.城市污水处理新技术[M].北京:中国建筑工业业出版社,1990
[7] Wilderer,P.A.,Franta J.R..Biological Treatment of Papermill Wastewater by Ssequencing Batch Reactor Technology to Reduce Residual Organics[J]. Water Science and Technology,1997,35(1):129-136
[8]刘永淞,陈纯.SBR法工艺特性研究[J].中国给水排水,1990,6(6): 5-11
[9]彭永臻,邵剑英,周利等.利用ORP作为SBR反应时间的计算机控制参数[J].中国给水排水.1997,13(6):6-9
[10]马小丽,王增长,侯安清.SBR工艺的发展与应用[J].山西建筑,2006, 32(1):188-189
[11]彭永臻.SBR法的五大优点[J].中国给水排水,1993,9(2):29-31
[12]方先金.SBR工艺特性及降解过程的研究[J].给水排水,2000,6(7): 18-21
[13] Jr, Lloyd H,Ketchum.Design and Physical Features of Sequencing Batch Reactors[J].Water Science and Technology,1997,35(1):11-18
[14] Fikret Kargi,Ahmet Uygur.Nutrient Removal Performance of a Sequencing Batch Reactor as a Function of the Sludge Age[J].Enzyme and Microbial Technology,2002,31(6):842-847
[15]李颖.SBR法在水污染治理中的应用[J].北京建筑工程学院学报,2002, 18(1):8-12
[16] Irvine,R.L.Sequencing Batch Biological Reactor-an Overview[J].JWPCF, 1997,51(2):235-243
[17] Arora.ML.Technology Evaluation of Sequencing Batch Reactor[J]. JWPCF,1985,57(8):867-870
[18]王福珍.污泥膨胀问题与序列间歇式活性污泥法[J].中国环境科学, 1996,17(1):65-67
[19]马小丽,王增长,侯安清.SBR工艺的发展与应用[J].山西建筑,2006, 32(1):188-189
[20] D. Obaja,S. Macé,J. Mata-Alvarez.Biological Nutrient Removal by a Sequencing Batch Reactor (SBR) Using an Internal Organic Carbon Source in Digested Piggery Wastewater[J].Bioresource Technology,2005,96(1):7-14
[21] R.Ganesh,G. Balaji,R.A. Ramanujam,Biodegradation of Tannery Wastewater Using Sequencing Batch Reactor—Respirometric Assessment[J]. Bioresource Technology,2006,97(15):1815-1821
[22]刘喜光,胡丽萍等.SBR法的主要设备及仪表研究[J].给水排水,1996, 22(11):20-22
[23]丁峰,彭永臻,董文艺.活性污泥法台泡沫问题的产生与控制技术[J].给水排水,2000,26(2):13-16
[24]唐受印,戴友芝等.水处理工程师手册[M].北京:化学工业出版社, 2000
[25] SLAMET A.Impact of Excessive Aeration on Biological Phosphorus Removal from Wastewater[J].Water Research,1998,32(1):200-208
[26]张可方.SBR法处理城市污水除磷效果及规律研究[J].广州大学学报(自然科学版),2003,2(4):353-356
[27]高宇.SBR生物除磷的研究进展[J].重庆工商大学学报(自然科学版), 2005,22(1):30-34
[28] Q. Fontenot,C. Bonvillain,M. Kilgen and R. Boopathy.Effects of Temperature,Salinity and Carbon:Nitrogen Ratio on Sequencing Batch Reactor Treating Shrimp Aquaculture Wastewater[J].Bioresource Technology,2007,98(9):1700-1703
[29] Meltem Sarioglu.Biological Phosphorus Removal in a Sequencing Batch Reactor by Using Pure Cultures[J].Process Biochemistry,2005,40(5): 1599-1603
[30]李秀玮,彭永臻,王淑莹等.以DO作为SBR法处理工业废水反应时间的控制参数[J].哈尔滨商业大学学报(自然科学版),2002,18(5):537-540
[31]汪大辉,雷乐成.水处理新技术及工程设计[M].北京:化学工业出版社,2001
[32]李淑更,张立秋,吴学伟等.ICEAS反应器处理城市污水的试验研究[J].广州大学学报,2004,3(4):361-368
[33]陈克玲,詹键.CAST工艺处理城市污水原理及设计[J].环境科学与技术,2004,27(4):71-73
[34]冯生华.澳大利亚IDEA工艺污水处理厂简介[J].给水排水,1996, 22(11):26-27
[35]魏永,闪红光.循环式活性污泥法(CASS)的研究进展[J].辽宁城乡环境科技,2004,24(4):7-10
[36]熊红权,李文彬.CASS工艺在国内的应用现状[J].中国给水排水,2003, 2(19):34-35
[37]杨波,陈兰.适用于中小城市污水处理的UNITANK技术[J].中国环保产业,2003,4:34-36
[38]詹伯军,陈国喜,方士等.皮革废水SBR工艺对比试验研究[J].污染防治技术,1998,11(3):134-136
[39]王乾扬,方士,陈国喜等.膜法SBR工艺处理皮革废水研究[J].中国给水排水,1999,15(3):54-56
[40]倪国,况武,缪应祺.厌氧序批式活性污泥工艺的研究及进展[J].环境科学动态,2003,3(1):37-39
[41]龙北生,孙大群,边德军等.采用两级SBR工艺优化除磷脱氮[J].给水排水,2003,29(11):34-37
[42]葛丽英,李功振,于林堂等.两级SBR工艺处理小城镇生活污水的试验研究[J].给水排水,2003,16(1):9-11
[43]冷成保,柳小荣,肖波.物化—水解酸化—SBR法处理淀粉废水[J].中国给水排水,2003,19(11):71-72
[44]罗锋,陈万志,熊忠等.ABR—SBR工艺处理高浓度纤维板有机有毒废水[J].环境污染治理技术与设备,2003,4(7):56-59
[45]程洁红,李尔熵.缺氧—SBR法—混凝法工艺处理垃圾渗滤液的试验研究[J].环境污染治理技术与设备,2003,4(5):77-79
[46]陈立波,黄有诚,柏承志.加压曝气—序批式活性污泥反应器(P-SBR)的研究[J].给水排水,2000,26(11):9-11
[47]刘军,王觉福,郭茜.PAC-SBR生物处理工艺在上海桃浦污水处理厂的应用[J].环境保护科学,1999,25(2):1-3
[48]陈郭建,魏兴义.PAC-SBR处理高浓度有机废水[J].环境工程,1995, 13(5):3-6
[49]乔蕴虹,赵心梅,谷兆全.寒冷地区活性污泥培养与强化实践[J].包头钢铁学院学报,2003,22(4):367-36
[50]管秀琼.SBR处理制浆中段废水活性污泥的培养驯化[J].环境保护, 2006,25(2):76-78
[51]傅金祥,腾险峰,李彤岩.低温下DAT-IAT工艺污水处理厂活性污泥培养驯化[J].沈阳建筑大学学报(自然科学报),2005,21(1):43-46
[52]陈滢,彭永臻,刘敏等.SBR法处理生活污水时非丝状菌污泥膨胀的发生与控制[J].环境科学学报,2005,25(1):105-108
[53] Peng Y Z,Gao C D,Wang S Y.Non-filamentous Sludge Bulking Caused by a Deficiency of Nitrogen in Industrial Wastewater Treatment[J].Water Science and Technology,2003,47(11):289-295
[54]王培冈,张冬梅,赵平健.SBR工艺用于生活污水脱氮除磷的试验研究[J].西安科技学院学报,2003,23(1):30-33
[55] Satoshi Tsuneda,Takashi Ohno,Koichi Soejima,Akira Hirata.Simultaneous Nitrogen and Phosphorus Removal Using Denitrifying Phosphate-accumulating Organisms in a Sequencing Batch Reactor[J].Biochemical Engineering Journal, 2006,27(3):91-196
[56]李健,陈双星,石凤林等.大型SBR工艺启动特点及活性污泥培养驯化[J].给水排水,2001,27(5):30-32
[57]徐慧,周利,王伟平.丝状菌性污泥膨胀的影响因素及控制方法[J].环境技术,2005,6(4):18-21
[58] B.S. Akin ,A.Ugurlu.Monitoring and Control of Biological Nutrient Removal in a Sequencing Batch Reactor[J].Process Biochemistry,2005, 40(8):2873-2878
[59]崔丽英.SBR法处理阿胶制药废水的应用研究[D].北京:北京交通大学,2004
[60]王平.水解酸化——PACT/SBR工艺处理光敏剂废水研究与工程实践[D].重庆:重庆大学,2004
[61]李飞龙.SBR法数学模型的研究[D].北京:北京工商大学,2003
[62]李本玉.SBR法处理酿酒废水的试验研究[D].江苏:江苏理工大学, 1999
[63]汤武平.食品废水的SBR技术研究[D].辽宁:东北大学,2002
[64]田海涛.水解——SBR工艺处理粪便污水研究[D].北京:北京交通大学,2004
[65]陈广春.SBR法处理木糖废水的动力学研究[D].四川:四川大学,2000
[66]王平.水解酸化—PACT/SBR工艺处理光敏剂废水研究与工程实践[D].重庆:重庆大学,2004
[67]李飞龙.SBR法数学模型的研究[D].北京:北京工商大学,2003
[68]李本玉.SBR法处理酿酒废水的试验研究[D].江苏:江苏理工大学, 1999
[69]王涛,楼上游.中国城市污水处理工艺现状调查与技术经济指标评价[J].给水排水,2004,30(5):1-4
[70]邓晓林,王国华,任鹤云.上海城市污水处理厂的污泥处置途径探讨[J].给水排水,2001,16(5):19-22
[71]刘永龄.从运转角度浅议城市污水处理厂的设计[J].给水排水,1995, 4(3):41-44
[72]杨敏,张建强,李亚澜.污水处理工程中节能问题的探讨[J].工业安全与环保,2005,31(2):22-24
[73]张晓明.污水处理设计中需探讨的问题[J].山西建筑,2003,29(1): 131-132
[74]黄伟.污水处理厂节能降耗的有效措施[J].河南化工,2002,1(1):46-46
[75]吴慧芳,孔火良.城镇小型生活污水处理设备及其展望[J].工业安全与环保,2003,29(5):17-20
[76]唐受印,戴友芝.水处理工程手册[M].北京:化学工业出版社,2004
[77]周金全.城市污水处理工艺设备及招标投标管理[M].北京:化学工业出版社,2003
[78]赵明,舒春敏.我国城市供水状况及节水对策[J].干旱区资源与环境, 2003,17(1):32-37
[79]高景峰,彭永臻,王淑莹.污水生物处理模糊控制的研究现状[J].环境科学与技术,2004,27(1):90-93
[80]陈振民.提高厌氧处理甲烷生成量方法的初步探讨[J].环境污染治理技术与设备,2004,5(5):43-47
[2]顾国维.水污染治理技术研究[M].上海:同济大学出版社,1997
[3]张自杰.排水工程(下)[M].北京:中国建筑工业出版社,1996
[4]赵丽珍,缪应棋.SBR技术的研究及进展[J].江苏理工大学学报,2001, 1(5):32-35
[5]沈耀良,王宝贞.废水生物处理新技术——理论与应用[M].北京:中国环境科学出版社,2001
[6]于彩霞.城市污水处理新技术[M].北京:中国建筑工业业出版社,1990
[7] Wilderer,P.A.,Franta J.R..Biological Treatment of Papermill Wastewater by Ssequencing Batch Reactor Technology to Reduce Residual Organics[J]. Water Science and Technology,1997,35(1):129-136
[8]刘永淞,陈纯.SBR法工艺特性研究[J].中国给水排水,1990,6(6): 5-11
[9]彭永臻,邵剑英,周利等.利用ORP作为SBR反应时间的计算机控制参数[J].中国给水排水.1997,13(6):6-9
[10]马小丽,王增长,侯安清.SBR工艺的发展与应用[J].山西建筑,2006, 32(1):188-189
[11]彭永臻.SBR法的五大优点[J].中国给水排水,1993,9(2):29-31
[12]方先金.SBR工艺特性及降解过程的研究[J].给水排水,2000,6(7): 18-21
[13] Jr, Lloyd H,Ketchum.Design and Physical Features of Sequencing Batch Reactors[J].Water Science and Technology,1997,35(1):11-18
[14] Fikret Kargi,Ahmet Uygur.Nutrient Removal Performance of a Sequencing Batch Reactor as a Function of the Sludge Age[J].Enzyme and Microbial Technology,2002,31(6):842-847
[15]李颖.SBR法在水污染治理中的应用[J].北京建筑工程学院学报,2002, 18(1):8-12
[16] Irvine,R.L.Sequencing Batch Biological Reactor-an Overview[J].JWPCF, 1997,51(2):235-243
[17] Arora.ML.Technology Evaluation of Sequencing Batch Reactor[J]. JWPCF,1985,57(8):867-870
[18]王福珍.污泥膨胀问题与序列间歇式活性污泥法[J].中国环境科学, 1996,17(1):65-67
[19]马小丽,王增长,侯安清.SBR工艺的发展与应用[J].山西建筑,2006, 32(1):188-189
[20] D. Obaja,S. Macé,J. Mata-Alvarez.Biological Nutrient Removal by a Sequencing Batch Reactor (SBR) Using an Internal Organic Carbon Source in Digested Piggery Wastewater[J].Bioresource Technology,2005,96(1):7-14
[21] R.Ganesh,G. Balaji,R.A. Ramanujam,Biodegradation of Tannery Wastewater Using Sequencing Batch Reactor—Respirometric Assessment[J]. Bioresource Technology,2006,97(15):1815-1821
[22]刘喜光,胡丽萍等.SBR法的主要设备及仪表研究[J].给水排水,1996, 22(11):20-22
[23]丁峰,彭永臻,董文艺.活性污泥法台泡沫问题的产生与控制技术[J].给水排水,2000,26(2):13-16
[24]唐受印,戴友芝等.水处理工程师手册[M].北京:化学工业出版社, 2000
[25] SLAMET A.Impact of Excessive Aeration on Biological Phosphorus Removal from Wastewater[J].Water Research,1998,32(1):200-208
[26]张可方.SBR法处理城市污水除磷效果及规律研究[J].广州大学学报(自然科学版),2003,2(4):353-356
[27]高宇.SBR生物除磷的研究进展[J].重庆工商大学学报(自然科学版), 2005,22(1):30-34
[28] Q. Fontenot,C. Bonvillain,M. Kilgen and R. Boopathy.Effects of Temperature,Salinity and Carbon:Nitrogen Ratio on Sequencing Batch Reactor Treating Shrimp Aquaculture Wastewater[J].Bioresource Technology,2007,98(9):1700-1703
[29] Meltem Sarioglu.Biological Phosphorus Removal in a Sequencing Batch Reactor by Using Pure Cultures[J].Process Biochemistry,2005,40(5): 1599-1603
[30]李秀玮,彭永臻,王淑莹等.以DO作为SBR法处理工业废水反应时间的控制参数[J].哈尔滨商业大学学报(自然科学版),2002,18(5):537-540
[31]汪大辉,雷乐成.水处理新技术及工程设计[M].北京:化学工业出版社,2001
[32]李淑更,张立秋,吴学伟等.ICEAS反应器处理城市污水的试验研究[J].广州大学学报,2004,3(4):361-368
[33]陈克玲,詹键.CAST工艺处理城市污水原理及设计[J].环境科学与技术,2004,27(4):71-73
[34]冯生华.澳大利亚IDEA工艺污水处理厂简介[J].给水排水,1996, 22(11):26-27
[35]魏永,闪红光.循环式活性污泥法(CASS)的研究进展[J].辽宁城乡环境科技,2004,24(4):7-10
[36]熊红权,李文彬.CASS工艺在国内的应用现状[J].中国给水排水,2003, 2(19):34-35
[37]杨波,陈兰.适用于中小城市污水处理的UNITANK技术[J].中国环保产业,2003,4:34-36
[38]詹伯军,陈国喜,方士等.皮革废水SBR工艺对比试验研究[J].污染防治技术,1998,11(3):134-136
[39]王乾扬,方士,陈国喜等.膜法SBR工艺处理皮革废水研究[J].中国给水排水,1999,15(3):54-56
[40]倪国,况武,缪应祺.厌氧序批式活性污泥工艺的研究及进展[J].环境科学动态,2003,3(1):37-39
[41]龙北生,孙大群,边德军等.采用两级SBR工艺优化除磷脱氮[J].给水排水,2003,29(11):34-37
[42]葛丽英,李功振,于林堂等.两级SBR工艺处理小城镇生活污水的试验研究[J].给水排水,2003,16(1):9-11
[43]冷成保,柳小荣,肖波.物化—水解酸化—SBR法处理淀粉废水[J].中国给水排水,2003,19(11):71-72
[44]罗锋,陈万志,熊忠等.ABR—SBR工艺处理高浓度纤维板有机有毒废水[J].环境污染治理技术与设备,2003,4(7):56-59
[45]程洁红,李尔熵.缺氧—SBR法—混凝法工艺处理垃圾渗滤液的试验研究[J].环境污染治理技术与设备,2003,4(5):77-79
[46]陈立波,黄有诚,柏承志.加压曝气—序批式活性污泥反应器(P-SBR)的研究[J].给水排水,2000,26(11):9-11
[47]刘军,王觉福,郭茜.PAC-SBR生物处理工艺在上海桃浦污水处理厂的应用[J].环境保护科学,1999,25(2):1-3
[48]陈郭建,魏兴义.PAC-SBR处理高浓度有机废水[J].环境工程,1995, 13(5):3-6
[49]乔蕴虹,赵心梅,谷兆全.寒冷地区活性污泥培养与强化实践[J].包头钢铁学院学报,2003,22(4):367-36
[50]管秀琼.SBR处理制浆中段废水活性污泥的培养驯化[J].环境保护, 2006,25(2):76-78
[51]傅金祥,腾险峰,李彤岩.低温下DAT-IAT工艺污水处理厂活性污泥培养驯化[J].沈阳建筑大学学报(自然科学报),2005,21(1):43-46
[52]陈滢,彭永臻,刘敏等.SBR法处理生活污水时非丝状菌污泥膨胀的发生与控制[J].环境科学学报,2005,25(1):105-108
[53] Peng Y Z,Gao C D,Wang S Y.Non-filamentous Sludge Bulking Caused by a Deficiency of Nitrogen in Industrial Wastewater Treatment[J].Water Science and Technology,2003,47(11):289-295
[54]王培冈,张冬梅,赵平健.SBR工艺用于生活污水脱氮除磷的试验研究[J].西安科技学院学报,2003,23(1):30-33
[55] Satoshi Tsuneda,Takashi Ohno,Koichi Soejima,Akira Hirata.Simultaneous Nitrogen and Phosphorus Removal Using Denitrifying Phosphate-accumulating Organisms in a Sequencing Batch Reactor[J].Biochemical Engineering Journal, 2006,27(3):91-196
[56]李健,陈双星,石凤林等.大型SBR工艺启动特点及活性污泥培养驯化[J].给水排水,2001,27(5):30-32
[57]徐慧,周利,王伟平.丝状菌性污泥膨胀的影响因素及控制方法[J].环境技术,2005,6(4):18-21
[58] B.S. Akin ,A.Ugurlu.Monitoring and Control of Biological Nutrient Removal in a Sequencing Batch Reactor[J].Process Biochemistry,2005, 40(8):2873-2878
[59]崔丽英.SBR法处理阿胶制药废水的应用研究[D].北京:北京交通大学,2004
[60]王平.水解酸化——PACT/SBR工艺处理光敏剂废水研究与工程实践[D].重庆:重庆大学,2004
[61]李飞龙.SBR法数学模型的研究[D].北京:北京工商大学,2003
[62]李本玉.SBR法处理酿酒废水的试验研究[D].江苏:江苏理工大学, 1999
[63]汤武平.食品废水的SBR技术研究[D].辽宁:东北大学,2002
[64]田海涛.水解——SBR工艺处理粪便污水研究[D].北京:北京交通大学,2004
[65]陈广春.SBR法处理木糖废水的动力学研究[D].四川:四川大学,2000
[66]王平.水解酸化—PACT/SBR工艺处理光敏剂废水研究与工程实践[D].重庆:重庆大学,2004
[67]李飞龙.SBR法数学模型的研究[D].北京:北京工商大学,2003
[68]李本玉.SBR法处理酿酒废水的试验研究[D].江苏:江苏理工大学, 1999
[69]王涛,楼上游.中国城市污水处理工艺现状调查与技术经济指标评价[J].给水排水,2004,30(5):1-4
[70]邓晓林,王国华,任鹤云.上海城市污水处理厂的污泥处置途径探讨[J].给水排水,2001,16(5):19-22
[71]刘永龄.从运转角度浅议城市污水处理厂的设计[J].给水排水,1995, 4(3):41-44
[72]杨敏,张建强,李亚澜.污水处理工程中节能问题的探讨[J].工业安全与环保,2005,31(2):22-24
[73]张晓明.污水处理设计中需探讨的问题[J].山西建筑,2003,29(1): 131-132
[74]黄伟.污水处理厂节能降耗的有效措施[J].河南化工,2002,1(1):46-46
[75]吴慧芳,孔火良.城镇小型生活污水处理设备及其展望[J].工业安全与环保,2003,29(5):17-20
[76]唐受印,戴友芝.水处理工程手册[M].北京:化学工业出版社,2004
[77]周金全.城市污水处理工艺设备及招标投标管理[M].北京:化学工业出版社,2003
[78]赵明,舒春敏.我国城市供水状况及节水对策[J].干旱区资源与环境, 2003,17(1):32-37
[79]高景峰,彭永臻,王淑莹.污水生物处理模糊控制的研究现状[J].环境科学与技术,2004,27(1):90-93
[80]陈振民.提高厌氧处理甲烷生成量方法的初步探讨[J].环境污染治理技术与设备,2004,5(5):43-47