A2/O+MBR工艺运行效果与碳排放特征研究

呼永锋, 梁梅, 张永祥, 王坤

中国环境科学 ›› 2021, Vol. 41 ›› Issue (9) : 4439-4446.

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中国环境科学 ›› 2021, Vol. 41 ›› Issue (9) : 4439-4446.
碳排放控制

A2/O+MBR工艺运行效果与碳排放特征研究

  • 呼永锋1, 梁梅2, 张永祥1, 王坤3
作者信息 +

Study on operation efficiency and carbon emission characteristics of A2/O + MBR process

  • HU Yong-feng1, LIANG Mei2, ZHANG Yong-xiang1, WANG Kun3
Author information +
文章历史 +

摘要

对北京市通州区H再生水厂采用的A2/O+MBR工艺运行效果与不同环节碳排放特征进行研究.结果表明:2018年该再生水厂对BOD5,CODcr,NH4+-N,TN和TP的平均去除率分别为97.3%,94.1%,98.6%,77.0%,96.2%;全厂碳排放总量和吨水碳排放量呈春夏季节逐渐降低,秋冬季节缓慢升高的特征,全厂综合吨水碳排放量约为2.26kgCO2e/t.碳排放总量中能耗碳排放量占主要地位,CH4,N2O和物耗碳排放量占比较小;统计分析显示CH4,能耗和物耗吨水碳排放量与BOD5,TN进水浓度及BOD5去除率显著相关;N2O吨水碳排放量与TN与BOD5进水浓度显著相关;直接,间接吨水碳排放量与水量无显著相关性.

Abstract

The operation effect and carbon emission characteristics of the A2/O+MBR process in the H reclaimed water plant of Tongzhou District, Beijing, were studied in this paper. The results showed that the average removal rates of BOD5, CODcr, NH4+-N, TN and TP were 97.3%, 94.1%, 98.6%, 77.0% and 96.2% respectively. The total carbon emission and carbon emission per ton of water of the H reclaimed water plant decreased gradually in spring and summer and increased slowly in autumn and winter, the total carbon emission per ton of water was about 2.26kgCO2e/t. In the total carbon emissions, energy consumption carbon emissions accounted for the leading position, while CH4, N2O carbon emissions, and drug consumption carbon emissions accounted for a relatively small proportion. The statistical analysis results showed that the carbon emissions of CH4 ton water, energy consumption ton water, and material consumption ton water were significantly correlated with BOD5, TN influent concentration, and BOD5 removal rate. The carbon emission of N2O per ton of water was significantly correlated with the influent concentrations of TN and BOD5. There is no significant correlation between direct and indirect carbon emissions per ton of water and water quantity.

关键词

A2/O+MBR工艺 / 碳排放 / 污水处理 / 运行效果

Key words

A2/O+MBR process / carbon emissions / operation effect / wastewater treatment

引用本文

导出引用
呼永锋, 梁梅, 张永祥, 王坤. A2/O+MBR工艺运行效果与碳排放特征研究[J]. 中国环境科学. 2021, 41(9): 4439-4446
HU Yong-feng, LIANG Mei, ZHANG Yong-xiang, WANG Kun. Study on operation efficiency and carbon emission characteristics of A2/O + MBR process[J]. China Environmental Science. 2021, 41(9): 4439-4446
中图分类号: X703   

参考文献

[1] 宋宝木,秦华鹏,马共强.污水处理厂运行阶段碳排放动态变化分析:以深圳某污水处理厂为例[J]. 环境科学与技术, 2015,38(10):204-209.Song B M, Qin H P, Ma G Q. Analysis for dynamic changes of wastewater treatment plant carbon emissions in operation phase:with a wastewater treatment plant in Shenzhen as an example[J]. Environmental Science & Technology, 2015,38(10):204-209.
[2] IPCC.2006IPCC Guidelines for national greenhouse gas inventories, intergovernmental panel on climate change 2006[M]. Cambridge:Cambridge University Press, 2006.
[3] Mamais D, Noutsopoulos C, Dimopoulou A, et al. Wastewater treatment process impact on energy savings and greenhouse gas emissions[J]. Water Science and Technology, 2015,71(2):303-308.
[4] Bao Z Y, Sun S C, Sun D Z. Characteristics of direct CO2 emissions in four full-scale wastewater treatment plants[J]. Desalination and Water Treatment, 2015,54(4/5):1070-1079.
[5] Malila R, Lehtoranta S, Viskari E L. The role of source separation in nutrient recovery-comparison of alternative wastewater treatment systems[J]. Journal of Cleaner Production, 2019,219:350-358.
[6] 王安,赵天忠.北京市废弃物处理温室气体排放特征[J]. 中国环境监测, 2017,33(2):68-75.Wang A, Zhao T Z. Greenhouse gas emission characteristics of municipal waste management in Beijing[J]. Environmental Monitoring in China, 2017,33(2):68-75.
[7] 翟萌,邵越,徐福军.西安污水处理厂温室气体排放及减排对策研究[J]. 环境工程, 2015,34(2):23-26.Zhai M, Shao Y, Xu F J. Countermeasures on greenhouse gas emission reduction for the wastewater treatment plants of Xi'an[J]. Environmental Engineering, 2015,34(2):23-26.
[8] Singh P, Kansal A, Carliell M C. Energy and carbon footprints of sewage treatment methods[J]. Journal of Environmental Management, 2016,165:22-30.
[9] Singh P, Kansal A. Energy and GHG accounting for wastewater infrastructure[J]. Resources, Conservation and Recycling, 2018,128:499-507.
[10] Zawartka P, Dorota B K, Agata B. Model of carbon footprint assessment for the life cycle of the system of wastewater collection, transport and treatment[J]. Scientific Reports, 2020,10(1):1-21.
[11] Bani S M, Yerushalmi L, Haghighat F. Estimation of greenhouse gas generation in wastewater treatment plants-model development and application[J]. Chemosphere, 2010,78(9):1085-1092.
[12] 谢淘,汪诚文.污水处理厂温室气体排放评估[J]. 清华大学学报(自然科学版), 2012,52(4):473-477.Xie T, Wang C W. Greenhouse gas emissions from wastewater treatment plants[J]. Journal of Tsinghua University (Science and Technology), 2012,52(4):473-477.
[13] 余娇,赵荣钦,肖连刚,等.基于"水-能-碳"关联的城市污水处理系统碳排放研究[J]. 资源科学, 2020,42(6):1052-1062.Yu J, Zhao R Q, Xiao L G, et al. Carbon emissions of urban wastewater treatment system based on the" water-energy-carbon" nexus[J]. Resources Science, 2020,42(6):1052-1062.
[14] 王晓莲,彭永臻,马勇,等.A2/O法污水生物脱氮除磷处理技术与应用[M]. 北京:科学出版社, 2012:21-24.Wang X L, Peng Y Z, Ma Y, et al. Treatment technology and application of biological nitrogen and phosphorus removal by A2/O method[M]. Beijing:Science Press, 2012:21-24.
[15] 张自杰.排水工程[M]. 4版.北京:中国建筑工业出版社, 2000:306-319.Zhang, Z J. Drainage engineering[M]. 4th Edition. Beijing:China Architecture and Building Press, 2000:306-319.
[16] 黄霞,文湘华.水处理膜生物反应器原理与应用[M]. 北京:科学出版社, 2012:1-16.Huang X, Wen X H. Principle and application of membrane bioreactor for water treatment[M]. Beijing:Science Press, 2012:1-16.
[17] 曹斌,黄霞,北中敦,等.A2/O-膜生物反应器强化生物脱氮除磷中试研究[J]. 中国给水排水, 2007,23(3):22-26.Cao B, Huang X, AtsushiKitanaka, et al. Pilot test on enhanced biological nitrogen and phosphorus removal by using A2/O-MBR[J]. China Water & Wasterwater, 2007,23(3):22-26.
[18] 严晓旭.基于CFD的膜生物反应器膜池水力学特性及其优化研究[D]. 北京:清华大学, 2016.Yan X X. Study on the hydrodynamics and its optimization of membrane tank in membrane bioreactor based on computational fluid dynamics[D]. Beijing:Tsinghua University, 2016.
[19] 杨群.低C/N比污水EMBR脱氮工艺研究[D]. 武汉:华中科技大学, 2011.Yang Q. Research on EMBR process for denitrigenation of the wastewater of low C/N ratio[D]. Wuhan:Huazhong University of Science and Technology, 2011.
[20] 张娇.电场耦合膜生物反应器膜污染控制和强化除磷研究[D]. 北京:清华大学, 2015.Zhang J. Fouling suppression and enhanced phosphorus removal in electro-membrane bioreactor[D]. Beijing:Tsinghua University, 2015.
[21] DB11/307-2013水污染物综合排放标准[S].DB11/307-2013 Integrated discharge standard of water pollutants[S].
[22] 国家环境保护总局编.水与废水监测分析方法[M]. 4版.北京:中国环境科学出版社, 2002.State Environmental Protection Administration. Standard methods for the examination of water and wastewater[M]. 4th Ed. Beijing:China Environmental Science Press, 2002.
[23] GB18918-2002城镇污水处理厂污染物排放标准[S].GB18918-2002 Discharge standard of pollutants for municipal wastewater treatment plant[S].

基金

京津冀水资源安全保障技术研发集成与示范应用(2016YFC0401404)

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