生物膜法A^2/O^2焦化废水处理系统缺氧反应器工艺特性  

Process characteristics of anoxic reactor in biofilm A^2/O^2 system treating coking wastewater

作　　者：李亚新[1] 赵义[1] 岳秀萍[1] 周鑫[1] 杨怀旺 杜金成 姚润生 马健安 

机构地区：[1]太原理工大学环境科学与工程学院,太原030024 [2]临汾同世达实业有限公司,山西临汾041000

出　　处：《工业用水与废水》2008年第1期15-19,共5页Industrial Water & Wastewater

基　　金：山西省科技攻关项目(2006031104-02)

摘　　要：以焦化厂废水处理系统气浮设备出水为试验废水水源,在中试规模上研究了生物膜法A2/O2(厌氧/缺氧/好氧/好氧)系统中缺氧反应器的工艺特性和效果。缺氧反应器为以陶粒作填料的上流式滤池。研究结果表明,缺氧反硝化对去除焦化废水中COD有重要作用。反硝化菌可利用一些好氧微生物和厌氧微生物都难以降解的焦化废水中的有机物作碳源,反硝化反应器可去除进水中40%的COD。缺氧反硝化反应器进水碳氮质量比在5以上就可基本满足焦化废水反硝化对碳源的需求。稳定运行状况下的NO3--N容积负荷不大于0.24 kg/(m3.d)。缺氧反应器的水力停留时间不小于24 h。系统进水COD、NH3-N的质量浓度分别在1 000～2 200、200～400 mg/L范围内,对系统进水不进行稀释的条件下,水解酸化反应器HRT为20 h,缺氧反应器HRT为24 h,一级好氧反应器和二级好氧反应器HRT均为48 h,二级好氧反应器硝化液回流比为3时,生物膜法A2/O2系统处理出水的COD和NH3-N可以同时达到《污水综合排放标准》(GB8978-1996)中的一级排放标准。With the effluent water from air-floating equipment of a coking wastewater treatment system as experimental source water, the process characteristics and effect of anoxic reactor in biofilm A^2/O^2（anaerobic/ anoxic/aerobic/aerobic） system was studied based on the pilot-scale experiment. Ceramic pellets were packed in the anoxic reactors with an upflow-filter mode. The results of the study indicated that, anoxic denitrification played a very important role in COD removal from coking wastewater. Denitrification bacteria could use some organic matters which could hardly be degraded by aerobic and anaerobic mierooganisms as carbon source, 40% of COD could be removed by the denitrification reactor. The carbon source could basicfly satisfy the need for the denitrification of coking wastewater so long as the influent carbon-nitrogen ratio was above 5. The NOB--N volume loading was lower than 0.24 kg/（m^3·d） under steady state operation. The hydraulic residence time of the anoxic reactor should be longer than 24 h. When the influent COD and NHB-N concentration of the system were 1 000 - 2 200, 200 - 400 mg/L respectively, with no dilution, the HRT of the hydrolytic acidification reactor, anoxic reactor, first-stage aerobic reactor and second-stage aerobic reactor were 20, 24, 48 and 48 h respectively, and at a nitrifying recirculation ratio of 3, the mass concentration of COD and NHB-N in effluent water treated by biofilm A^2/O^2 system could meet the specification for grade 1 in intergrated wastewater discharge standard （GB 8978-1996）.

关 键 词：焦化废水 生物膜法 厌氧/缺氧/好氧/好氧 反硝化 缺氧降解 

分 类 号：X703.1[环境科学与工程—环境工程] X784