| 开工过程对重整催化剂初期反应性能的影响 |
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| 引用本文： | 林晓峰.开工过程对重整催化剂初期反应性能的影响[J].炼油技术与工程,2003,33(5):48-51. |
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| 作者姓名： | 林晓峰 |
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| 作者单位： | 中国石油天然气股份有限公司大连石化分公司,辽宁省大连市,116032 |
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| 摘 要： | 对大连石化分公司采用CB-ll／CB—8催化剂两段装填的重整装置第一、二周期的开工过程及催化剂初期反应性能进行了比较，分析了开工过程条件不同，如开工时装置中的水含量、开工时间、催化剂还原时采用的氯气质量等，对催化剂初期反应性能造成的影响，说明了按规程要求开工的重要性。
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| 关 键 词： | 开工过程 重整催化剂 初期反应性能 催化重整装量 |
| 修稿时间： | 2002年8月6日 |
INFLUENCE OF START UP PROCESS ON PRIMARY CATALYST REACTION PERFORMANCE |
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| Lin Xiaofeng Dalian Petrochemical Company,PetroChina Company Limited.INFLUENCE OF START UP PROCESS ON PRIMARY CATALYST REACTION PERFORMANCE[J].Petroleum Refinery Engineering,2003,33(5):48-51. |
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| Authors: | Lin Xiaofeng Dalian Petrochemical Company PetroChina Company Limited |
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| Abstract: | The first/second period start up processes of the two stage reformer adopting CB 11/CB 8 catalyst in Dalian Company have been compared together with the primary catalyst reaction performance. Influence of water content in the unit under different start up conditions, start up time and the hydrogen quality of catalyst revivification on the primary catalyst reaction performance has been analyzed. Start up in accordance with the regulation requirement is emphasized. |
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| Keywords: | catalytic reformer on stream reforming catalyst activity |
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