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两种制革废水生化处理组合工艺的效能比较
引用本文:李建政,陈青松,柯伟士,李尧.两种制革废水生化处理组合工艺的效能比较[J].科技导报(北京),2011,29(22):68-71.
作者姓名:李建政  陈青松  柯伟士  李尧
作者单位:1. 城市水资源与水环境国家重点实验室;哈尔滨工业大学市政环境工程学院,哈尔滨 150090;2. 福建省百林环保技术有限公司,福建泉州 362271
基金项目:黑龙江省发展高新技术产业化项目(FW09C01); 哈尔滨市科技创新人才研究专项(2009RFXXS004)
摘    要: 借助于实际工程的运行,比较了水解酸化与序批式活性污泥法(SBR)组合工艺(H-SBR)和接触氧化与SBR组合工艺(O-SBR)两套设施处理制革废水的效能。结果表明,接触氧化与SBR组合工艺能有效处理制革废水,在接触氧化HRT 24h、SBR曝气5-7h的条件下,COD和氨氮平均去除率可分别达到83%和74%,出水平均浓度分别为273和42mg/L。采用水解酸化与SBR的组合工艺对预处理后的制革废水进行处理,在水解酸化HRT 24h、SBR曝气5-7h的条件下,COD和氨氮平均去除率分别仅为70%和5%,虽然COD可降低到500mg/L以下,但氨氮高达163mg/L左右,且需配套臭气处理设施。

关 键 词:制革废水    水解酸化    接触氧化    SBR    氨氮

Efficiency Evaluation of Two Combined Processes for Treating Tannery Wastewater
LI Jianzheng,CHEN Qingsong,KE Weishi,LI Yao . State Key Laboratory of Urban Water Resource , Environment,School of Municipal , Enviroment Engineering,Harbin Institute of Technology,Harbin ,China . Bailin Environmental Technology Co.,Ltd.,Quanzhou ,Fujian Province,China.Efficiency Evaluation of Two Combined Processes for Treating Tannery Wastewater[J].Science & Technology Review,2011,29(22):68-71.
Authors:LI Jianzheng  CHEN Qingsong  KE Weishi  LI Yao State Key Laboratory of Urban Water Resource  Environment  School of Municipal  Enviroment Engineering  Harbin Institute of Technology  Harbin  China Bailin Environmental Technology Co  Ltd  Quanzhou  Fujian Province  China
Institution:1. State Key Laboratory of Urban Water Resource and Environment; School of Municipal and Enviroment Engineering, Harbin Institute of Technology, Harbin 150090, China;2. Bailin Environmental Technology Co., Ltd.,Quanzhou 362271, Fujian Province, China
Abstract:Two processes used to treat organic wastewater discharged from a tannery are discussed and their treatment efficiencies are compared. The results show that the process of sequencing the batch reactor (SBR) combined with the contact oxidation (O-SBR) is more realistic than that of SBR combined with the hydrolysis acidification (H-SBR). With HRT contact oxidation for 24h and sewage aeration for 5-7h in the SBR, the average removal of 83% for COD and 74% for ammonia are achieved in the O-SBR process. The COD and ammonia in the effluent of the O-SBR process are about 273mg/L and 42mg/L, respectively. With HRT contact oxidation for 24h and the same sewage aeration in the SBR, the average removal of COD and ammonia are only 70% and 5%, respectively, in the H-SBR process. Though the COD is less than 500 mg/L, the ammonia is as high as 163mg/L in the effluent. Furthermore, an attached process to the H-SBR has to be constructed for fetor collection, transfer and treatment.
Keywords:tannery wastewater  hydrolytic acidification  biological contact oxidation  SBR  ammonia nitrogen  
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