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多相催化臭氧氧化法处理甲萘酚废水
引用本文:王利平,刘兵昌,蔡华,严文瑶. 多相催化臭氧氧化法处理甲萘酚废水[J]. 中国给水排水, 2009, 25(23)
作者姓名:王利平  刘兵昌  蔡华  严文瑶
作者单位:江苏工业学院,环境与安全工程学院,江苏,常州,213164
基金项目:常州科教城科研基金资助重点项目,常州市社会发展科技计划项目 
摘    要:以活性炭为载体、钾为助催化剂,采用浸渍法制备了Cu-K/AC催化剂,并考察了该催化剂催化臭氧氧化处理甲萘酚废水的效能.结果表明,当甲萘酚废水的COD为3 000 mg/L、含油量为120 mg/L时,在室温、pH=3、反应时间为120 min、催化剂投量为100 g/L、臭氧流量为5.2mg/min的条件下,催化臭氧氧化对COD及油类物质的去除率分别达到了93%和98%;臭氧氧化和催化臭氧氧化对COD的降解过程均符合表观一级反应动力学方程.

关 键 词:Cu-K/AC催化剂  臭氧氧化  甲萘酚废水

Heterogeneous Catalytic Ozonation Process for Treatment of Wastewater from 1-naphthol Production
WANG Li-ping,LIU Bing-chang,CAI Hua,YAN Wen-yao. Heterogeneous Catalytic Ozonation Process for Treatment of Wastewater from 1-naphthol Production[J]. China Water & Wastewater, 2009, 25(23)
Authors:WANG Li-ping  LIU Bing-chang  CAI Hua  YAN Wen-yao
Abstract:Taking activated carbon as carrier and potassium as cocatalyst, the Cu-K/AC catalyst was prepared by impregnating process. The efficiency of this catalyst for treating wastewater from 1-naph-thol production was investigated in catalytic ozonation process. The results show that the removal rates of COD and oil can reach 93% and 98% under the conditions of COD of 3 000 mg/L, initial oil concentra-tion of 120 mg/L, ambient temperature, pH of 3, reaction time of 120 min, catalyst dosage of 100 g/L and ozone of 5.2 mg/min. The degradation of COD by ozonation and catalytic ozonation conforms to the first-order reaction kinetics equation.
Keywords:Cu-K/AC catalyst  ozonation  wastewater from 1-naphthol production
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