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臭氧协同催化剂处理炼油废水实验研究
引用本文:崔金久.臭氧协同催化剂处理炼油废水实验研究[J].石油化工高等学校学报,2012,25(2):24-28.
作者姓名:崔金久
作者单位:宁波市环境保护科学研究设计院,浙江宁波,315012
摘    要:利用臭氧催化氧化技术,开展降解炼油废水的实验研究。通过模拟活性污泥法验证污水生物降解性能的调控效果。结果表明:利用臭氧非均相催化技术可有效降解炼油废水中有机污染物且生物降解性能显著提高,COD平均去除率达65.0%,BOD5/COD从0.13提高至0.28;对于本实验装置,处理4 000mL炼油废水最佳反应条件为臭氧流量40L/h,催化剂为200cm3载铜活性炭,pH=11,反应时间40min。

关 键 词:臭氧催化氧化  载铜活性炭  炼油废水  生物降解性能

Degradation of Refinery Wastewater by Ozonation Combined With Catalytic Technology
CUI Jin-jiu.Degradation of Refinery Wastewater by Ozonation Combined With Catalytic Technology[J].Journal of Petrochemical Universities,2012,25(2):24-28.
Authors:CUI Jin-jiu
Affiliation:CUI Jin-jiu(Ningbo Municipal Research & Design Institute of Environmental Protection,Ningbo Zhejiang 315012,P.R.China)
Abstract:The efficiency of catalytic ozonation on treating refinery wastewater was investigated and a simulated activated sludge process was conducted to determine the biodegradability improvement.The experimental results show that the heterogeneous catalyst of copper loaded activated carbon combined ozonation is effective on degrading the organic pollutants and improving the biodegradability of refinery wastewater.When treating 4 000 mL wastewater,the average COD removal rate of 65.0% is attained while the BOD5/COD rate is improved from 0.13 to 0.28,under the optimal operational conditions of pH 11,ozone flow rate 40 L/h,catalyst quantity 200 cm3 and reaction time 40 min.
Keywords:Catalytic ozonation  Copper loaded activated carbon  Refinery wastewater  Biodegradability
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