| SD-1、SD-2在汽油加氢精制装置预反应器中的首次工业应用 |
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| 引用本文： | 张斌,邓潇,龙斌,朱红林,许庆国.SD-1、SD-2在汽油加氢精制装置预反应器中的首次工业应用[J].化工科技市场,2008,31(8). |
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| 作者姓名： | 张斌 邓潇 龙斌 朱红林 许庆国 |
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| 作者单位： | 1. 大庆石化分公司炼油厂,黑龙江大庆,163711
2. 大庆石化公司工程公司 |
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| 摘 要： | SD-1、SD-2是中国石油大庆化工研究中心开发的新一代石蜡加氢催化剂,2008年1月,因大庆石化公司炼油厂汽油加氢装置精制装置预反应器压差升高,需更新催化剂,但汽油加氢精制催化剂DZG-10缺货,经技术分析,装入石蜡加氢催化剂SD-1、SD-2,运行2月内,床层压差上升平稳,产品质量合格.
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| 关 键 词： | 汽油加氢 系统压差 自硫化 结垢 |
Initial industrial application of SD-1 and SD-2 as gasoline hydrotreating catalysts in pre-reactor |
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| Zhang Bin,Deng Xiao,Long Bin,Zhu Honglin,Xu Qingguo.Initial industrial application of SD-1 and SD-2 as gasoline hydrotreating catalysts in pre-reactor[J].Chemical Technology Market,2008,31(8). |
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| Authors: | Zhang Bin Deng Xiao Long Bin Zhu Honglin Xu Qingguo |
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| Institution: | Zhang Bin~1 Deng Xiao~2 Long Bin~1 Zhu Honglin~1 Xu Qingguo~1The Refinery of Daqing PetroChemical Company,Daqing 163711,China,.Daqing PetroChemical Engineering Company |
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| Abstract: | SD-1 and SD-2 are new paraffin hydrogenation catalysts which were developed by Petrochina Company's Chemical Research Center of Daqing.Pre-reactor has to replace catalyst,because the pre-reactor differ pressure In- creased in January 2008.But the gasoline hydrotreating catalysts DZG-10 was out,it was replaced by catalyst SD-1 and SD-2 through the technical analysis.The bed differ pressure was rising steadily,and the products quality was qualified to standards after two month's running. |
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| Keywords: | gasoline hydrogenation system pressure sulfiding-self scaling |
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