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A~2/O~2生物膜工艺处理焦化废水研究
引用本文:郑俊,李红丽,张诗华. A~2/O~2生物膜工艺处理焦化废水研究[J]. 中国给水排水, 2009, 25(21)
作者姓名:郑俊  李红丽  张诗华
作者单位:1. 安徽工业大学,建筑工程学院,安徽,马鞍山,243002;华骐环保科技发展有限公司,安徽,马鞍山,243061
2. 安徽工业大学,建筑工程学院,安徽,马鞍山,243002
摘    要:采用A~2/O~2生物膜工艺处理焦化废水,分别考察了厌氧(A_1)、缺氧(A_2)、一级好氧(O_1)和二级好氧(O_2)反应器对污染物的去除效果.在A_1、A_2、O_1和O_2反应器的HRT分别为15.5、15、12、12 h,水温为20~30℃,pH值为7.0~9.5,回流比为3.0的条件下,各反应器对COD的平均去除率分别为31.0%、27.6%、48.1%和8.2%;在A1中NH_3-N浓度增加了25.2%,A_2、O_1、O_2反应器对NH_3-N的平均去除率分别为6.2%、46.7%和76.7%;系统出水COD、NH_3-N的平均浓度分别为227、11.5 mg/L,对COD、NH_3-N的平均去除率分别为87.2%、94.1%.

关 键 词:A2/O2工艺  生物膜反应器  厌氧  焦化废水

Treatment of Coke Plant Wastewater by Biofilm Reactor Based on A~2/O~2 Process
ZHENG Jun,LI Hong-li,ZHANG Shi-hua. Treatment of Coke Plant Wastewater by Biofilm Reactor Based on A~2/O~2 Process[J]. China Water & Wastewater, 2009, 25(21)
Authors:ZHENG Jun  LI Hong-li  ZHANG Shi-hua
Abstract:The A~2/O~2 biofilm process was used to treat coke plant wastewater, and the removal efficiencies of pollutants by anaerobic reactor A_1 , anoxic reactor A_2, one-stage aerobic reactor O_1 and twostage aerobic reactor O_2 were investigated respectively. When HRT of A_1, A_2, O_1 and O_2 reactors is 15.5 h, 15 h, 12 h and 12 h respectively, the water temperature is 20 to 30 ℃, pH is 7.0 to 9.5 and the reflux ratio is 3.0, the average removal rate of COD in the reactors is 31.0%, 27.6%, 48.1% and 8.2% respectively. The increment of ammonia nitrogen is 25.2% in A_1 reactor, and the average removal rates of ammonia nitrogen in other reactors are 6.2%, 46.7% and 76.7% respectively. The average concentrations of COD and ammonia nitrogen in the system effluent are 227 mg/L and 11.5 mg/L respectively,and the average removal rates of COD and ammonia nitrogen are 87.2% and 94.1% respectively.
Keywords:A~2/O~2 process  biofilm reactor  anaerobic treatment  coke plant wastewater
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