| 催化燃烧法处理炼油厂隔油池废气 |
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| 引用本文： | 刘忠生,王新,陈玉香,林大泉,单石灵,唐旭东.催化燃烧法处理炼油厂隔油池废气[J].化工环保,2001,21(3):152-155. |
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| 作者姓名： | 刘忠生 王新 陈玉香 林大泉 单石灵 唐旭东 |
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| 作者单位： | 1. 抚顺石油化工研究院,
2. 广州石油化工总厂, |
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| 摘 要： | 在隔油池废气催化燃烧处理中试装置上 ,采用蜂窝状 Pt、Pd、Ce多组分催化剂 ,在空速 40 0 0 0 h- 1 、反应器入口温度 2 5 0℃以上、进气总烃体积分数 10 0 0× 10 - 6 ～ 6 0 0 0× 10 - 6 条件下 ,可以使总烃去除率达到 96 %～ 99% ,净化排气总烃体积分数小于 10 0× 10 - 6 ,无恶臭气味
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| 关 键 词： | 隔电池 废气处理 催化燃烧 炼油厂 |
| 文章编号： | 1006-1878(2001)03-0152-04 |
| 修稿时间： | 2000年8月15日 |
Pilot Study on Catalytic Combustion of Waste Gas from Oil Separating Tank in Refinery Plant |
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| LIU Zhongsheng,WANG Xin,Chen Yuxiang,LIN Daquan,SHAN Shiling,TANG Xudong.Pilot Study on Catalytic Combustion of Waste Gas from Oil Separating Tank in Refinery Plant[J].Environmental Protection of Chemical Industry,2001,21(3):152-155. |
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| Authors: | LIU Zhongsheng WANG Xin Chen Yuxiang LIN Daquan SHAN Shiling TANG Xudong |
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| Abstract: | The pilot study on catalytic combustion of waste gas from oil separating tank was conducted with honeycomb multicomponent catalyst (composed of Pt,Pd,Ce).Under the conditions of 40000 h-1 of velocity,250℃ at the reactor inlet,the volume fraction of total hydrocarbon was decreased from 1000×10-6～6000×10-6 to less than 100×10-6 and its removal rate is 96%～99%.Purified gas is without any offensive odor. |
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| Keywords: | oil separating tank waste gas catalytic combustion |
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