| 催化裂解多产丙烯技术工业化试验装置设计 |
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| 引用本文： | 刘艳苹,丁洪春,龙钰. 催化裂解多产丙烯技术工业化试验装置设计[J]. 当代化工, 2011, 40(1): 100-103 |
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| 作者姓名： | 刘艳苹 丁洪春 龙钰 |
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| 作者单位： | 中国石油工程建设公司华东设计分公司,山东,青岛,266071;中国石油工程建设公司华东设计分公司,山东,青岛,266071;中国石油工程建设公司华东设计分公司,山东,青岛,266071 |
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| 摘 要： | 介绍了国内外第一套催化裂解多产丙烯技术(TMP)工业化试验装置的改造设计内容及投产后的运行情况.标定结果表明,大庆常压渣油经两段提升管催化裂解反应,在丙烯的收率达到20.38%的情况下,总液收为82.95%,而干气+焦炭产率只有13.99%.在多产丙烯的同时,兼顾汽油和柴油的质量.
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| 关 键 词： | TMP 催化裂解 丙烯 混合C4 |
Design of Commercial Test Unit of Catalytic Cracking Technology for Maximizing Propylene Yield |
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| LIU Yan-ping,DING Hong-chun,LONG Yu. Design of Commercial Test Unit of Catalytic Cracking Technology for Maximizing Propylene Yield[J]. Contemporary Chemical Industry, 2011, 40(1): 100-103 |
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| Authors: | LIU Yan-ping DING Hong-chun LONG Yu |
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| Affiliation: | LIU Yan-ping,DING Hong-chun,LONG Yu(CPECC East-China Design Branch,Shandong Qingdao 266071,China) |
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| Abstract: | Design content of reforming the domestic first commercial test unit adopting catalytic cracking technology for maximizing propylene yield(TMP) was introduced as well as operation conditions after reformation.The results show that through catalytic cracking reaction of Daqing atmospheric residue in two-stage riser,yield of propylene reaches 20.38%,total liquid yield is 82.95%,and yield of dry gas and coke is only 13.99%,which proves that TMP can maximize propylene yield without cost of light oil quality. |
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| Keywords: | TMP Catalytic cracking Propylene Mix C4 |
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