| 生产清洁汽油组分并增产丙烯的催化裂化工艺 |
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| 引用本文： | 许友好,张久顺,马建国,龙军.生产清洁汽油组分并增产丙烯的催化裂化工艺[J].石油炼制与化工,2004,35(9):1-4. |
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| 作者姓名： | 许友好 张久顺 马建国 龙军 |
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| 作者单位： | 石油化工科学研究院,北京,100083 |
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| 摘 要： | 生产汽油组分满足欧Ⅲ排放标准,又能增产丙烯的流化催化裂化工艺--MIP-CGP,在多产异构烷烃的催化裂化工艺基础上被提出。依据生产方案要求,研究了工艺条件和开发专用催化剂CGP-1,并在中型试验装置上进行该工艺探索试验。中型试验结果表明,在该反应系统中,用大庆重质原料油,可以生产出烯烃体积分数低于18％的汽油,同时还能生产丙烯,产率达9.20％。
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| 关 键 词： | 催化裂化 汽油料 烯烃 丙烯 |
| 修稿时间： | 2004年2月12日 |
CATALYTIC CRACKING TECHNOLOGY FOR PRODUCING NAPHTHA WITH CLEAN GASOLINE COMPOSITION AND INCREASING PROPYLENE |
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| Xu Youhao,Zhang Jiushun,Ma Jianguo,Long Jun.CATALYTIC CRACKING TECHNOLOGY FOR PRODUCING NAPHTHA WITH CLEAN GASOLINE COMPOSITION AND INCREASING PROPYLENE[J].Petroleum Processing and Petrochemicals,2004,35(9):1-4. |
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| Authors: | Xu Youhao Zhang Jiushun Ma Jianguo Long Jun |
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| Abstract: | A FCC technology for producing naphtha with clean gasoline composition and increasing propylene, dubbed MIP-CGP, based on MIP technology was proposed. According to the requirement of production scheme, tests were conducted on the pilot plant and operating parameters were investigated with Daqing heavy feedstock over a newly developed proprietary catalyst named CGP-1. The results showed that under the selected operating conditions, the olefin content in the cracked naphtha was below 18%, and the propylene yield was up to 9. 20%. |
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| Keywords: | catalytic cracking gasoiine stock olefin propylene |
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