| RGD-C催化剂在林源重油催化裂化装置上的工业应用 |
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| 引用本文： | 徐言彪,王义东,李岩冰,王国辉. RGD-C催化剂在林源重油催化裂化装置上的工业应用[J]. 石油炼制与化工, 2003, 34(9): 32-35 |
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| 作者姓名： | 徐言彪 王义东 李岩冰 王国辉 |
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| 作者单位： | 大庆炼化公司,大庆,163411 |
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| 摘 要： | 在设计处理量为0．85Mt／a、加工大庆常压渣油的FCC装置上采用长岭炼油化工有限责任公司催化剂厂生产的多产液化气和柴油催化剂RGD-C，配合部分粗汽油回炼技术，可以使液化气、0号柴油的收率分别增加2．23和4．6个百分点，在催化剂单耗0．95kg／t的情况下，可将汽油中的烯烃含量降到35％左右。
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| 关 键 词： | 催化裂化装置 重油 RGD-C催化剂 渣油 汽油 回炼技术 大庆炼化公司林源生产区 |
| 修稿时间： | 2002-12-20 |
COMMERCIAL APPLICATION OF RGD-C CATALYST IN LINYUAN HEAVY OIL FCCU |
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| Xu Yanbiao,Wang Yidong,Li Yanbing,Wang Guohui. COMMERCIAL APPLICATION OF RGD-C CATALYST IN LINYUAN HEAVY OIL FCCU[J]. Petroleum Processing and Petrochemicals, 2003, 34(9): 32-35 |
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| Authors: | Xu Yanbiao Wang Yidong Li Yanbing Wang Guohui |
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| Abstract: | RGD-C catalyst manufactured by Changling Catalyst Works for increasing LPG and LCO was applied in the 0. 85Mt/a heavy oil FCCU for processing Daqing atmospheric residue. Combined with part of naphtha recycle, the yields of LPG and LCO increased by 2. 23 and 4. 6 percentages respec-tively. At a catalyst makeup rate of 0. 95kg/t, the olefin content in naphtha reduced to about 35%. |
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| Keywords: | atmospheric residue catalytic cracking catalyst gasoline stock liquefied petroleum gas light cycle oil olefin |
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