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生物处理组合工艺用于制革废水处理
引用本文:于勇, 丁然, 田秉晖, 高迎新, 张昱, 杨敏, 宫兆波. 生物处理组合工艺用于制革废水处理[J]. 环境工程学报, 2017, 11(6): 3375-3380. doi: 10.12030/j.cjee.201603217
作者姓名:于勇  丁然  田秉晖  高迎新  张昱  杨敏  宫兆波
作者单位:1. 中国科学院生态环境研究中心环境水质学国家重点实验室, 北京 100085; 2. 中国科学院大学, 北京 100049; 3. 新疆克拉玛依实验检测研究院水质中心, 克拉玛依 834000
基金项目:国家水体污染控制与治理科技重大专项(2012ZX07203-003-R05) 国家自然科学基金面上项目(51178448) 天津市科技计划项目(15YFYSSF00040)
摘    要:针对制革废水高COD、高总氮的问题,提出了基于上流式厌氧污泥床(UASB)、上流式反硝化污泥床(UDNSB)、生物接触氧化池的生物处理组合工艺,进行了为期321 d的现场中试研究。研究结果表明,对于COD、TN、NH4+-N平均浓度分别为2 740、278和193 mg·L-1的制革废水,在硝化液回流比R为300%,UASB反应器、UDNSB反应器、生物接触氧化池的水力停留时间(HRT)分别为11、22和57 h,平均容积负荷分别为5.63 kg COD·(m3·d)-1、0.30 kg TN·(m3·d)-1和0.11 kg NH4+-N·(m3·d)-1的条件下,该组合工艺处理出水COD、TN和NH4+-N的平均浓度分别为190、69.8和4.6 mg·L-1,其平均去除率分别达到92%、73%和97%以上。

关 键 词:制革废水   上流式厌氧污泥床(UASB)   上流式反硝化污泥床(UDNSB)   生物接触氧化池
收稿时间:2016-05-20

Tannery wastewater treatment with biological treatment combined process
YU Yong, DING Ran, TIAN Binghui, GAO Yingxin, ZHANG Yu, YANG Min, GONG Zhaobo. Tannery wastewater treatment with biological treatment combined process[J]. Chinese Journal of Environmental Engineering, 2017, 11(6): 3375-3380. doi: 10.12030/j.cjee.201603217
Authors:YU Yong  DING Ran  TIAN Binghui  GAO Yingxin  ZHANG Yu  YANG Min  GONG Zhaobo
Affiliation:1. State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, China; 2. University of Chinese Academy of Sciences, Beijing 100049, China; 3. Water Quality Center, Xinjiang Karamay Experimental Detection Research Insitute, Karamay 834000, China
Abstract:Tannery wastewater is characterized by high concentrations of chemical oxygen demand (COD) and total nitrogen (TN).In this study, a combined biological treatment process based on an up-flow anaerobic sludge blanket (UASB), an up-flow denitrification sludge blanket (UDNSB), and a biological contact oxidation pond was proposed to treat tannery wastewater.A pilot wastewater treatment system was operated for 321 days, with efficient removal rates of COD, TN, and NH4+-N.The hydraulic retention times (HRTs) of the UASB, UDNSB, and biological contact oxidation pond were 11, 22, and 57 h, respectively, and the corresponding volumetric loadings were 5.63 kg COD·(m3·d)-1, 0.30 kg TN·(m3·d)-1, and 0.11 kg NH4+-N·(m3·d)-1, with a nitrification liquid reflux ratio (R) of 300%.Average concentrations of COD, TN, and NH4+-N in the tannery wastewater were 2 740, 278, and 193 mg·L-1, respectively.After the combined biological treatment, the average concentrations of COD, TN, and NH4+-N in the final effluent were 190, 69.8, and 4.6 mg·L-1, with removal rates of more than 92%, 73%, and 97%, respectively.
Keywords:tannery wastewater  up-flow anaerobic sludge blanket (UASB)  up-flow denitrification sludge blanket (UDNSB)  biological contact oxidation pond
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