MBBR处理城市生活废水的污染物降解动力学

丁杰, 龚钰涵, 刘先树. MBBR处理城市生活废水的污染物降解动力学[J]. 环境工程学报, 2016, 10(10): 5359-5365. doi: 10.12030/j.cjee.201602039
引用本文: 丁杰, 龚钰涵, 刘先树. MBBR处理城市生活废水的污染物降解动力学[J]. 环境工程学报, 2016, 10(10): 5359-5365. doi: 10.12030/j.cjee.201602039
DING Jie, GONG Yuhan, LIU Xianshu. Kinetics of pollutant degradation in MBBR treating domestic wastewater[J]. Chinese Journal of Environmental Engineering, 2016, 10(10): 5359-5365. doi: 10.12030/j.cjee.201602039
Citation: DING Jie, GONG Yuhan, LIU Xianshu. Kinetics of pollutant degradation in MBBR treating domestic wastewater[J]. Chinese Journal of Environmental Engineering, 2016, 10(10): 5359-5365. doi: 10.12030/j.cjee.201602039

MBBR处理城市生活废水的污染物降解动力学

  • 基金项目:

    国家水体污染控制与治理科技重大专项(2013ZX07201007)

    新世纪优秀人才支持计划(NCET-11-0795)

  • 中图分类号: X703.1

Kinetics of pollutant degradation in MBBR treating domestic wastewater

  • Fund Project:
  • 摘要: 采用一种新开发的多孔流动态悬浮填料结合自主设计的高效移动床生物膜反应器(moving bed biofilm reactor)处理城市生活废水并利用Lawrence-McCarty模型建立该系统的污染物降解动力学方程组,考察系统对有机物、氨氮、总氮的降解速率及去除效果与微生物量之间的关系。结果表明,有机物、氨氮、总氮降解动力学方程的出水浓度模拟值与实际废水处理后的出水浓度测量值拟合度良好,绝对误差分别为0.03~0.13、0.05~0.68、0.06~0.56。其中,有机物降解动力学方程的动力学常数为vmax=7.18 d-1,KS=84.67 mg·L-1(以COD计),明显高于普通活性污泥法动力学常数的一般参考值,说明MBBR系统处理生活污水中有机污染物的降解速率和去除效果优于活性污泥法。
  • 加载中
  • [1] 于龙,赵雅芝,童健,等.MBBR处理制药废水的试验研究.环境科学与技术,2007,30(3):66-67YU Long,ZHAO Yazhi,TONG Jian,et al.Performance of MBBR in treating pharmaceutical wastewater.Environmental Science & Technology,2007,30(3):66-67(in Chinese)
    [2] 师永健,张耀斌,全燮,等.移动床生物膜反应器用于苯酚废水处理的性能研究.环境科学学报,2013,33(1):30-35SHI Yongjian,ZHANG Yaobin,QUAN Xie,et al.Performance of moving bed biofilm reactor in removal of phenol from artificial wastewater.Acta Scientiae Circumstantiae,2013,33(1):30-35(in Chinese)
    [3] 季民,杨造燕,薛广宁,等.移动床生物膜反应器在污水处理中的应用研究.城市环境与城市生态,2000,13(3):47-49JI Min,YANG Zaoyan,XUE Guangning,et al.Wastewater treatment in the moving bed biofilm process.Urban Environment & Urban Ecology,2000,13(3):47-49(in Chinese)
    [4] 季民,薛广宁,董广瑞,等.移动床生物膜反应器处理生活污水.中国给水排水,2003,19(2):56-57JI Min,XUE Guangning,DONG Guangrui,et al.Use of moving bed biofilm reactor for domestic wastewater treatment.China Water & Wastewater,2003,19(2):56-57(in Chinese)
    [5] 于洪斌,全燮,丁蕴铮,等.MBBR处理生活、生产混合污水.中国给水排水,2005,21(1):49-52YU Hongbin,QUAN Xie,DING Yunzheng,et al.Moving bed biofilm reactor for treatment of mixed domestic and industrial wastewater.China Water & Wastewater,2005,21(1):49-52(in Chinese)
    [6] BARWAL A,CHAUDHARY R.To study the performance of biocarriers in moving bed biofilm reactor (MBBR) technology and kinetics of biofilm for retrofitting the existing aerobic treatment systems:A review.Reviews in Environmental Science and Bio/Technology,2014,13(3):285-299
    [7] 王学江,夏四清,陈玲,等.DO对MBBR同步硝化反硝化生物脱氮影响研究.同济大学学报(自然科学版),2006,34(4):514-517WANG Xuejiang,XIA Siqing,CHEN Ling,et al.Effect of DO on simultaneous nitrification and denitrification in MBBR.Journal of Tongji University (Natural Science),2006,34(4):514-517(in Chinese)
    [8] 汪传新,龚灵潇,彭永臻.低温下MBBR处理低碳氮质量比生活污水的同步硝化反硝化特性.中南大学学报(自然科学版),2014,45(8):2920-2927WANG Chuanxin,GONG Lingxiao,PENG Yongzhen.Characteristics of simultaneous nitrification-denitrification in MBBR treating domestic sewage with low C/N ratio at low temperature.Journal of Central South University (Science and Technology),2014,45(8):2920-2927(in Chinese)
    [9] LEYVA-DÍAZ J.C.,GONZÁLEZ-MARTÍNEZ A.,GONZÁLEZ-LÓPEZ J.,et al.Kinetic modeling and microbiological study of two-step nitrification in a membrane bioreactor and hybrid moving bed biofilm reactor-membrane bioreactor for wastewater treatment.Chemical Engineering Journal,2015,259:692-702
    [10] FERRAI M.,GUGLIELMI G.,ANDREOTTOLA G.Modelling respirometric tests for the assessment of kinetic and stoichiometric parameters on MBBR biofilm for municipal wastewater treatment.Environmental Modelling & Software,2010,25(5):626-632
    [11] ZHU Yan,ZHANG Yan,REN Hongqiang,et al.Physicochemical characteristics and microbial community evolution of biofilms during the start-up period in a moving bed biofilm reactor.Bioresource Technology,2015,180:345-351
    [12] ALMSTRAND R.,DAIMS H.,PERSSON F.,et al.New methods for analysis of spatial distribution and coaggregation of microbial populations in complex biofilms.Applied and Environmental Microbiology,2013,79(19):5978-5987
    [13] 东秀珠,蔡妙英.常见细菌系统鉴定手册.北京:科学出版社,2001:349-418
    [14] 国家环境保护总局.水和废水监测分析方法.4版.北京:中国环境科学出版社,2002:103
    [15] 方建文,刘建广,郝兆亮.悬浮填料好氧移动床反应器挂膜启动方式研究.环境科学导刊,2010,29(1):11-14 FANG Jianwen,LIU Jianguang,HAO Zhaoliang.Study on startup methods of biofilm culturing of suspended carrier aerobic moving bed reactor.Environmental Science Survey,2010,29(1):11-14(in Chinese)
    [16] 苑泉.城市污水厂尾水MBBR深度脱氮技术及微生物群落特征.北京:中国环境科学研究院硕士学位论文,2015 YUAN Quan.Denitrification MBBRs technology and microbial characteristics for advanced nitrogen removal of wastewater treatment plant effluent.Beijing:Master Dissertation of Chinese Research Academy of Environmental Sciences,2015(in Chinese)
    [17] IBRAHIM H.T.Y.缺氧/好氧移动床生物膜反应器处理城市污水的效能研究.重庆:重庆大学博士学位论文,2014 IBRAHIM H.T.Y.Research on the performance of anoxic/aerobic moving bed biofilm reactors for domestic wastewater treatment.Chongqing:Doctor Dissertation of Chongqing University,2014(in Chinese)
    [18] VAN HAANDEL A.C.,VAN DER LUBBE J.G.M.Handbook of Biological Wastewater Treatment:Design and Optimisation of Activated Sludge Systems.2nd ed.London:IWA Publishing,2012:359
    [19] PLATTES M.,HENRY E.,SCHOSSELER P.M.,et al.Modelling and dynamic simulation of a moving bed bioreactor for the treatment of municipal wastewater.Biochemical Engineering Journal,2006,32(2):61-68
    [20] 施汉昌,邱勇.污水生物处理的数学模型与应用.北京:中国建筑工业出版社,2014:34-53
    [21] 马建勇,张兴文,杨凤林,等.移动床生物膜反应器处理低浓度污水的性能.大连理工大学学报,2003,43(1):46-50 MA Jianyong,ZHANG Xingwen,YANG Fenglin,et al.Treating low concentration wastewater by moving bed biofilm reactor.Journal of Dalian University of Technology,2003,43(1):46-50(in Chinese)
    [22] 张忠华,汤兵,赵一宁,等.移动床生物膜反应器的启动及影响因素的研究.水处理技术,2012,38(11):84-89 ZHANG Zhonghua,TANG Bing,ZHAO Yining,et al.Start-up and its influence factors in moving bed biofilm reactor.Technology of Water Treatment,2012,38(11):84-89(in Chinese)
    [23] 王京城.MBBR处理中低温生活污水动力学研究.绿色科技,2015(5):182-183 WANG Jingcheng.Study on kinetics of treating low temperature domestic sewage in MBBR.Journal of Green Science and Technology,2015(5):182-183(in Chinese)
  • 加载中
计量
  • 文章访问数:  2447
  • HTML全文浏览数:  1934
  • PDF下载数:  473
  • 施引文献:  0
出版历程
  • 收稿日期:  2016-04-01
  • 刊出日期:  2016-10-20

MBBR处理城市生活废水的污染物降解动力学

  • 1. 哈尔滨工业大学市政环境工程学院, 哈尔滨 150093
基金项目:

国家水体污染控制与治理科技重大专项(2013ZX07201007)

新世纪优秀人才支持计划(NCET-11-0795)

摘要: 采用一种新开发的多孔流动态悬浮填料结合自主设计的高效移动床生物膜反应器(moving bed biofilm reactor)处理城市生活废水并利用Lawrence-McCarty模型建立该系统的污染物降解动力学方程组,考察系统对有机物、氨氮、总氮的降解速率及去除效果与微生物量之间的关系。结果表明,有机物、氨氮、总氮降解动力学方程的出水浓度模拟值与实际废水处理后的出水浓度测量值拟合度良好,绝对误差分别为0.03~0.13、0.05~0.68、0.06~0.56。其中,有机物降解动力学方程的动力学常数为vmax=7.18 d-1,KS=84.67 mg·L-1(以COD计),明显高于普通活性污泥法动力学常数的一般参考值,说明MBBR系统处理生活污水中有机污染物的降解速率和去除效果优于活性污泥法。

English Abstract

参考文献 (23)

目录

/

返回文章
返回