生物吸附-多级A/O-活性焦组合工艺对污水中氮磷及有机污染物的去除

王东, 王小东, 朱引, 沈斐, 李激, 王硕. 生物吸附-多级A/O-活性焦组合工艺对污水中氮磷及有机污染物的去除[J]. 环境工程学报, 2018, 12(7): 1907-1916. doi: 10.12030/j.cjee.201712110
引用本文: 王东, 王小东, 朱引, 沈斐, 李激, 王硕. 生物吸附-多级A/O-活性焦组合工艺对污水中氮磷及有机污染物的去除[J]. 环境工程学报, 2018, 12(7): 1907-1916. doi: 10.12030/j.cjee.201712110
WANG Dong, WANG Xiaodong, ZHU Yin, SHEN Fei, LI Ji, WANG Shuo. Removal of organic contaminants,nitrogen,phosphorus by combined adsorption-multistage A/O-activated coke process[J]. Chinese Journal of Environmental Engineering, 2018, 12(7): 1907-1916. doi: 10.12030/j.cjee.201712110
Citation: WANG Dong, WANG Xiaodong, ZHU Yin, SHEN Fei, LI Ji, WANG Shuo. Removal of organic contaminants,nitrogen,phosphorus by combined adsorption-multistage A/O-activated coke process[J]. Chinese Journal of Environmental Engineering, 2018, 12(7): 1907-1916. doi: 10.12030/j.cjee.201712110

生物吸附-多级A/O-活性焦组合工艺对污水中氮磷及有机污染物的去除

  • 基金项目:

    国家水体污染控制与治理科技重大专项(2015ZX07306001-05, 2017ZX07202001-01)

Removal of organic contaminants,nitrogen,phosphorus by combined adsorption-multistage A/O-activated coke process

  • Fund Project:
  • 摘要: 利用生物吸附(biological absorption,AB)-多级缺氧/好氧(anaerobic/oxic,A/O)-活性焦滤池组合工艺对城市污水进行处理研究。结果表明:该组合工艺出水COD、TN、TP平均浓度为20、8.5、0.25 mg·L-1,对COD、TN、TP平均去除率为95%、76.5%、80%,3个工艺段对有机污染物的平均去除率分别为55%、26%、14%。其中生物吸附段主要去除粒径较大的颗粒态有机物,多级A/O段可以去除进水中53%左右溶解性有机物;活性焦滤池利用活性焦丰富的中孔结构有效吸附多级A/O出水中难生物降解的芳香类及环烷类有机物。该组合工艺能实现高标准出水、高效脱氮除磷、能源节约、资源回收,是具有良好应用前景的污水处理工艺。
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  • [1] 宋旭,孙士宇,张伟,等. “水污染防治行动计划”实施背景下我国水环境管理优化对策研究[J]. 环境保护科学,2017,43(2):51-57. 10.16803/j.cnki.issn.1004-6216.2017.02.010
    [2] SARMADI M, MORTEZAEIFAR S,KERMANI M,et al.Performance evaluation of wastewater treatment plant system (MBR) of Semnan Industry Park in industrial effluent recovery[J].Iran Occupational Health,2017,14(1):165-175
    [3] NIU K,JIANG Y M,WEI W,et al.Problems and countermeasures of AB process in Zibo wastewater treatment plant[J].Water & Wastewater Engineering,2004,30(2):27-29
    [4] 潘宁,石淑倩,柯崇宜,等. 吸附生物降解法(AB工艺)A段反应机理分析[J]. 环境工程,2000,18(4):21-23
    [5] 郑凯凯,支尧,王东,等. 生物吸附/MBR/硫铁自养反硝化组合工艺运行特性及蛋白质源污泥增量研究[J]. 环境科学学报,2017,37(8):3003-3009 10.13671/j.hjkxxb.2017.0021
    [6] 刘胜军,杨学,石凤,等. 多段多级AO除磷脱氮工艺分析与研究[J]. 给水排水,2012,48(S1):191-194
    [7] 张国珍,高小波,武福平,等. 流量分配比对改良型多级A/O工艺去除污染物的影响[J]. 环境工程学报,2016,10(3):1165-1170
    [8] 王文相,刘继先,李涛,等. 石家庄市桥西污水处理厂一期升级改造工程设计[J]. 中国给水排水,2016,10(16):50-54
    [9] 杨少斌,刘凯. 西安市第二污水处理厂升级改造工程设计[J]. 中国给水排水,2016,32(10):48-51
    [10] 王启涛. 潍坊市污水处理厂升级改造工艺的运行探讨[J]. 中国给水排水,2012,28(2):56-58
    [11] RIVERAUTRILLA J,SANCHEZPOLO M,GOMEZSERRANO V,et al.Activated carbon modifications to enhance its water treatment applications: An overview[J].Journal of Hazardous Materials,2011,187(1):1-23 10.1016/j.jhazmat.2011.01.033
    [12] XU J,HUANG X,SUI X,et al.Assessment and modeling of a sequential process for water treatment: Adsorption and batch CWAO regeneration of activated carbon[J].Industrial & Engineering Chemistry Chemical & Engineering Data,2012,51:8867-8874 10.1021/ie2020312
    [13] BHATNAGAR A,HOGLAND W,MARQUES M,et al.An overview of the modification methods of activated carbon for its water treatment applications[J].Chemical Engineering Journal,2013,219(3):499-511 10.1016/j.cej.2012.12.038
    [14] IBRAHIM A H.Utilization of coconut fibre carbon in the removal of soluble petroleum fraction polluted water[J].International Journal of Physicalences,2007,2(2):47-49
    [15] 李若征,杨宏,靳昕,等. 活性焦对典型煤气化废水的吸附及其影响因素[J]. 环境污染与防治,2016,38(1):19-22
    [16] 王东,庞之鹏,沈斐,等. 活性焦对垃圾渗滤液中难降解有机物的吸附及影响因素研究[J]. 环境科学学报,2017,37(12):4653-4661 10.13671/j.hjkxxb.2017.0238
    [17] 滕济林,姜艳,曹效鑫,等. 粉末活性焦强化A/A/O工艺处理煤气化废水的中试研究[J]. 环境科学学报,2014,34(5):1249-1255 10.13671/j.hjkxxb.2014.0194
    [18] KUAI L,VREESE I D,VANDEVICERE P,et al.GAC-amended UASB reactor for the stable treatment of toxic textile wastewater[J].Environmental Technology Letters,1998,19(11):1111-1117
    [19] 陈金声,史家梁,徐亚同. 硝化速率测定和硝化细菌计数考察脱氮效果的应用[J]. 上海环境科学,1996,15(3):18-20
    [20] 沈翼军,吴瑒,张新喜. 不同测定条件对于活性污泥反硝化速率测定的影响[J].山东化工, 2016,45(5):7-11
    [21] 张晓霞. 温度对生物除磷系统的处理性能及种群关系影响研究[D]. 西安:西安建筑科技大学,2015
    [22] 孙月鹏.多级AO工艺处理低碳源污水的试验研究[D]. 邯郸:河北工程大学,2014
    [23] CZERWIONKA K,MAKINIA J.Dissolved and colloidal organic nitrogen removal from wastewater treatment plants effluents and reject waters using physical-chemical processes[J].Water Science & Technology,2014,70(3):561-568 10.2166/wst.2014.267
    [24] LI W,HUA T,ZHOU Q,et al.Treatment of stabilized landfill leachate by the combined process of coagulation/flocculation and powder activated carbon adsorption[J].Desalination,2010,264(1/2):56-62 10.1016/j.desal.2010.07.004
    [25] 朱文倩,徐斌,林琳,等. 微污染水源中溶解性有机氮组成规律及其水处理特性[J]. 中国环境科学,2014,34(1):130-135
    [26] 孔海霞,袁林江,王晓昌. 活性污泥对污水中有机物、铵和磷酸盐的生物吸附试验研究[J]. 西安建筑科技大学学报(自然科学版),2007,39(5):735-740
    [27] 曹贵华,王淑莹,彭永臻,等. 流量分配比对改良A/O分段进水脱氮除磷特性的影响[J]. 化工学报,2012,63(4):1249-1257
    [28] ANTHEUNISSE J,KOENE J I A.Alteration of the aerobic- and facultative anaerobic bacterial flora of the A/B purification process caused by limited oxygen supply[J].Water Research,1987,21(1):129-131 10.1016/0043-1354(87)90108-4
    [29] 仝坤. 褐煤活性焦吸附难降解有机废水研究进展[J]. 油气田环境保护,2016,26(5):44-47
    [30] 李绍秀,彭勃. 污水处理厂AB法工艺改造方案的探讨[J]. 工程建设与设计,2006(4):54-56
    [31] OEHMEN A,LEMOS P C,CARVALHO G,et al.Advances in enhanced biological phosphorus removal: From micro to macro scale[J].Water Research,2007,41(11):2271-2300
    [32] KUBA T,LOOSDRECHT M, HEIJNEN J.Phosphorus and nitrogen removal with minimal COD requirement by integration of denitrifying dephosphatation and nitrification in a two-sludge system[J].Water Research,1996,30(7):1702-1710
    [33] KUMAGAI T,INOUE T,et al.Influences of drugs on the oxygen uptake rate and biosorption of activated sludge[J].Biological & Pharmaceutical Bulletin,2006,29(1):183-186
    [34] 沈翼军,吴瑒,杨殿海,等. 运行方式对厌氧区碳源分流多级A/O工艺处理效果的影响[J]. 环境污染与防治,2016,38(11):25-30
    [35] DASTGHEIB S A, KARANFIL T, CHENG W.Tailoring activated carbons for enhanced removal of natural organic matter from natural waters[J].Carbon,2004,42(3):547-557 10.1016/j.carbon.2003.12.062
    [36] QUINLIVAN P A,LI L,KNAPPE D R.Effects of activated carbon characteristics on the simultaneous adsorption of aqueous organic micropollutants and natural organic matter[J].Water Research,2005,39(8):1663-1673 10.1016/j.watres.2005.01.029
    [37] 孟冠华,李爱民,张全兴. 活性炭的表面含氧官能团及其对吸附影响的研究进展[J].离子交换与吸附,2007,23(1):88-94
    [38] TONG K,LIN A,JI G,et al.The effects of adsorbing organic pollutants from super heavy oil wastewater by lignite activated coke[J].Journal of Hazardous Materials,2016,308:113-119 10.1016/j.jhazmat.2016.01.014
    [39] 靳昕,滕济林,赵立,等. 臭氧强化曝气生物滤池处理生化尾水试验研究[J].环境工程,2014,32 (s1):372-375
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  • 刊出日期:  2018-07-26

生物吸附-多级A/O-活性焦组合工艺对污水中氮磷及有机污染物的去除

  • 1. 江南大学环境与土木工程学院,无锡 214122
  • 2. 无锡市环境监测中心站,无锡 214122
  • 3. 江苏省厌氧生物技术重点实验室,无锡 214122
  • 4. 江苏高校水处理技术与材料协同创新中心,苏州 215009
基金项目:

国家水体污染控制与治理科技重大专项(2015ZX07306001-05, 2017ZX07202001-01)

摘要: 利用生物吸附(biological absorption,AB)-多级缺氧/好氧(anaerobic/oxic,A/O)-活性焦滤池组合工艺对城市污水进行处理研究。结果表明:该组合工艺出水COD、TN、TP平均浓度为20、8.5、0.25 mg·L-1,对COD、TN、TP平均去除率为95%、76.5%、80%,3个工艺段对有机污染物的平均去除率分别为55%、26%、14%。其中生物吸附段主要去除粒径较大的颗粒态有机物,多级A/O段可以去除进水中53%左右溶解性有机物;活性焦滤池利用活性焦丰富的中孔结构有效吸附多级A/O出水中难生物降解的芳香类及环烷类有机物。该组合工艺能实现高标准出水、高效脱氮除磷、能源节约、资源回收,是具有良好应用前景的污水处理工艺。

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