|本期目录/Table of Contents|

[1]吕龙刚,展学成,陈明林,等.裂解碳五选择性加氢催化剂LY-9801 F的工业应用[J].石化技术与应用,2024,1:64-66.
 L? Long-gang,ZHAN Xue-cheng,CHEN Ming-lin,et al.Industrial application of selective hydrogenation catalyst LY-9801 F for pyrolysis C5[J].Petrochemical technology & application,2024,1:64-66.
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裂解碳五选择性加氢催化剂LY-9801 F的工业应用(PDF)

《石化技术与应用》[ISSN:1009-0046/CN:62-1138/TQ]

期数:
2024年1期
页码:
64-66
栏目:
出版日期:
2024-01-10

文章信息/Info

Title:
Industrial application of selective hydrogenation catalyst LY-9801 F for pyrolysis C5
文章编号:
1009-0045(2024)01-0064-03
作者:
吕龙刚展学成陈明林李若愚孙利民马好文
中国石油石油化工研究院 兰州化工研究中心,甘肃 兰州 730060
Author(s):
L?譈 Long-gangZHAN Xue-chengCHEN Ming-linLI Ruo-yuSUN Li-minMA Hao-wen
Lanzhou Petrochemical Research Center,Petrochemical Research Institute,PetroChina,Lanzhou 730060,China
关键词:
裂解碳五选择性加氢钯系催化剂异戊二烯2-甲基-2-丁烯
Keywords:
pyrolysis C5selective hydrogenationPd-based catalystisoprene2-methyl-2-butene
分类号:
TE 624.43
DOI:
DOI:10.19909/j.cnki.ISSN1009-0045.2024.01.0064
文献标识码:
B
摘要:
为了将裂解碳五馏分中的二烯烃选择性加氢转化为单烯烃,开发出高选择性碳五加氢钯系催化剂LY-9801 F,并在8 kt/a碳五选择加氢装置上实现了工业应用。结果表明:在加氢反应器入口压力为0.4~0.8 MPa,入口温度为25~45 ℃,新鲜料体积空速为0.42~0.62 h-1,产品循环比为(25~32)∶1的工艺条件下,加氢产品中异戊二烯质量分数为0.09%~0.83%,二烯烃质量分数低于1.0%,其他二烯烃均已加氢转化,异戊二烯加氢转化率和2-甲基-2-丁烯选择性均大于85%,可满足工业装置运行要求。
Abstract:
In order to convert the dienes into monoolefins in cracked C5 fraction, selectively, Pd-based catalyst LY-9801 F for C5 selective hydrogenation was developed and used in a 8 kt/a C5 selective hydrogenation unit. The results showed that under the process conditions of reaction pressure 0.4-0.8 MPa, reactor inlet temperature 25-45 ℃, fresh material volume space velocity 0.42-0.62 h-1, and circulation ratio of products (25-32)∶1, the mass fraction of isoprene in the products was 0.09%-0.83%, the mass fraction of diene was less than 1.0%, the conversion rate of isoprene and the selectivity of 2-methyl-2-butene was more than 85%, which could meet the operation requirement of the industry unit.

参考文献/References

[1] 李宇静,梅相银.对乙烯产能成为全球第一的思考[J].中国石油和化工产业观察,2023(2):36-39.[2] 马好文,沈卫军,康宏敏,等.C5馏分在我国的加氢利用研究进展[J].现代化工,2011,31(Z 2):29-32.[3] 王军.国内裂解C5产业链发展现状及趋势[J].现代化工,2019,39(8):1-6.[4] 何龙,冯靓婧,赵存胜.Pd/Ca-Al2O3催化剂的制备及其C5抽余油加氢反应性能研究[J].石油炼制与化工,2018,49(9):64-68.[5] 吕龙刚,王宗宝,梁顺琴,等.裂解碳五馏分加氢生产乙烯裂解原料的研究[J].石化技术与应用,2014,32(4):307-309.[6] 田保亮,戴伟,杨志钢,等.裂解碳五双烯烃选择加氢[J].化工进展,2009,28(11):1932-1935. [7] 刘明晖,曾佑富,翁惠新,等.裂解碳五选择性加氢研究[J].精细石油化工,2006(3):26-28.[8] 马鸣,田保亮,杨志钢.裂解碳五馏分选择加氢催化剂的研究[J].石油化工,2009,38(10):1044-1047.[9] 郑彦彬,黄星亮.镍基催化剂催化模型化合物中异戊二烯加氢性能[J].石油化工,2003(12):1024-1027.

备注/Memo

备注/Memo:
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更新日期/Last Update: 2024-01-10