| RC031连续重整催化剂的工业试生产 |
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| 引用本文： | 刘安军,许浩洋,潘锦程. RC031连续重整催化剂的工业试生产[J]. 工业催化, 2009, 17(6): 39-41. DOI: 10.3969/j.issn.1008-1143.2009.06.009 |
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| 作者姓名： | 刘安军 许浩洋 潘锦程 |
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| 作者单位： | 1.中国石化催化剂分公司湖南建长石化公司，湖南 岳阳 414012;;2.中国石化石油化工科学研究院，北京 100083 |
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| 摘 要： | 在不降低RC031（生产型号）催化剂比表面积的情况下，可实现降低高铂型连续重整催化剂积炭速率和提高芳烃收率。催化剂的工业试生产结果表明，在反应条件相同情况下，与原有高铂型连续重整催化剂相比，具有选择性高、积炭速率低、水热稳定性好、持氯性能强和再生性能优良等特点。连续重整装置在不增加再生能力的前提下，可以在更高苛刻度或更高处理量下操作，最大限度地增加装置的经济效益。
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| 关 键 词： | 催化剂工程 连续重整 积炭速率 选择性 工业试生产 |
Commercial trial production of RC031 continuous reforming catalyst |
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| LIU Anjun,XU Haoyang,PAN Jincheng. Commercial trial production of RC031 continuous reforming catalyst[J]. Industrial Catalysis, 2009, 17(6): 39-41. DOI: 10.3969/j.issn.1008-1143.2009.06.009 |
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| Authors: | LIU Anjun XU Haoyang PAN Jincheng |
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| Affiliation: | （1.Hunan Jianchang Petrochemical Co., Ltd, Sinopec Catalyst Company, Yueyang 414012，Hunan, China; 2. Sinopec Research Institute of Petroleum Processing, Beijing 10083，China |
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| Abstract: | In order to reduce coke formation rate and improve yield of aromatics without loss of surface area, a RC031 continuous catalytic reforming(CCR) catalyst with high platinum content was developed. Commercial trial production results of the catalyst showed that, compared with existing high platinum CCR catalysts, RC031 exhibited higher selectivity, lower coke formation rate, excellent hydrothermal stability, strong chlorine retaining capability and good regenerability, which enabled the CCR unit to be operated under harsher condition and higher processing capacity without increasing regeneration demand, thereby maximized the economics. |
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| Keywords: | continuous reforming coke formation rate selectivity commercial trial production catalyst engineering |
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