| 炼油污水处理场恶臭污染及其治理研究 |
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| 引用本文： | 刘忠生,郭兵兵,王玉亭,刘念曾.炼油污水处理场恶臭污染及其治理研究[J].石油学报(石油加工),2003,19(1):79-83. |
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| 作者姓名： | 刘忠生 郭兵兵 王玉亭 刘念曾 |
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| 作者单位： | FushunResearchInstituteofPetroleumandPetrochemicals,Fushun113001,China |
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| 摘 要： | Main malodor pollutants from oil separator of Refinery A are hydrocarbons and a small quantity of sulfides.Main malodor pollutants from surface aeration tank of Refinery B are sulfides,especially CH3SH.And main malodor pollutants from bubbling aeration tank of Refinery C are also sulfides,of which H2S concentration is the highest,Catalytic combustion technology is applied to treat malodorous gas from oil separator of Refinery A,in which the total hydrocarbon removal was over 97%.The purified gas meets the national standard.Activated carbon adsorption is used to treat malodorous gas from surface aeration tank of Refinery B,and main pollutant CH3SH removal reached up to 98%-100%.As for malodorous gas from bubbling aeration tank of Refinery C,biopacking tower is used and the removals of hydrogen sulfide,organic sulfides and benzene series reached up to 80%-98%.
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| 关 键 词： | 炼油污水处理场 恶臭污染 污染治理 研究 |
MALODOR POLLUTION FROM REFINERY SEWAGE TREATMENT SYSTEM AND TREATMENT TECHNOLOGY |
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| LIU Zhong-sheng,GUO Bing-bing,WANG Yu-ting,Liu Nian-zeng.MALODOR POLLUTION FROM REFINERY SEWAGE TREATMENT SYSTEM AND TREATMENT TECHNOLOGY[J].Acta Petrolei Sinica (Petroleum Processing Section),2003,19(1):79-83. |
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| Authors: | LIU Zhong-sheng GUO Bing-bing WANG Yu-ting Liu Nian-zeng |
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| Abstract: | Main malodor pollutants from oil separator of Refinery A are hydrocarbons and a small quantity of sulfides. Main malodor pollutants from surface aeration tank of Refinery B are sulfides, especially CH3SH. And main malodor pollutants from bubbling aeration tank of Refinery C are also sulfides, of which H2S concentration is the highest. Catalytic combustion technology is applied to treat malodorous gas from oil separator of Refinery A, in which the total hydrocarbon removal was over 97%. The purified gas meets the national standard. Activated carbon adsorption is used to treat malodorous gas from surface aeration tank of Refinery B, and main pollutant CH3SH removal reached up to 98%～100%. As for malodorous gas from bubbling aeration tank of Refinery C, bio-packing tower is used and the removals of hydrogen sulfide, organic sulfides and benzene series reached up to 80%～98%. |
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| Keywords: | sewage treatment system malodor catalytic combustion activated carbon biological treatment |
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