|本期目录/Table of Contents|

[1]严巍宁,段佳辉,唐显全,等.降低重整汽油终馏点的二甲苯塔侧线气相抽出[J].石化技术与应用,2023,3:215-219.
 YAN Wei-ning,DUAN Jia-hui,TANG Xian-quan,et al.Using side-line gas phase extraction in xylene tower to reduce final distillation point of reformed gasoline[J].Petrochemical technology & application,2023,3:215-219.
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降低重整汽油终馏点的二甲苯塔侧线气相抽出(PDF)

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

期数:
2023年3期
页码:
215-219
栏目:
出版日期:
2023-05-10

文章信息/Info

Title:
Using side-line gas phase extraction in xylene tower to reduce final distillation point of reformed gasoline
文章编号:
1009-0045(2023)03-0215-05
作者:
严巍宁段佳辉唐显全胡晓彬
(大连西太平洋石油化工有限公司,辽宁 大连116600)
Author(s):
YAN Wei-ningDUAN Jia-huiTANG Xian-quanHU Xiao-bin
(Dalian West Pacific Petrochemical Co Ltd, Dalian 116600,China)
关键词:
连续重整二甲苯塔侧线气相抽出重整汽油终馏点能耗
Keywords:
continuous catalytic reformingxylene towerside-line gas phase extraction final distillation point of reformed gasolineenergy consumption
分类号:
TE 624.42;TE 626.21
DOI:
DOI:10.19909/j.cnki.ISSN1009-0045.2023.03.0215
文献标识码:
B
摘要:
介绍了大连西太平洋石油化工有限公司1.5 Mt/a连续重整装置降低重整汽油终馏点的二甲苯塔侧线气相抽出技术改造情况。结果表明:技术改造后,重整汽油的终馏点降低了约40 ℃,研究法辛烷值均值保持在101.0左右,有效提升了装置调和汽油的品质及比例,使催化汽油收率提高了2个百分点;该技术改造既没影响二甲苯塔的分馏精度,也未增加二甲苯组分的损失量,还使二甲苯塔进料温度提高了20 ℃,装置总能耗较技改前降低了366.40 MJ/h。
Abstract:
The technical modification of side-line gas phase extraction in the xylene tower to reduce the final distillation point of the reformed gasoline of the 1.5 Mt/a continuous catalytic reforming unit in Dalian West Pacific Petrochemical Co Ltd was introduced. The results showed that the final distillation point of the gasoline reduced by about 40 ℃,and the average research octane number(RON) kept up at about 101.0,which effectively enhanced the quality and proportion of the reformed gasoline,and increased the yield of the catalytic gasoline by 2 percentage points. The technical modification neither affected the fractionation accuracy of xylene tower,nor increased the loss of xylene component. Moreover,the feed temperature of xylene tower increased by 20 ℃,and the total energy consumption of the unit reduced by 366.40 MJ/h, compared with that before the technical modification.

参考文献/References

[1] 简建超,孙浩,冯海春. 汽油+芳烃型重整装置原料组分的优化[J]. 炼油技术与工程,2017,47(6):36-39.[2] 兰晓光. 颗粒白土在芳烃精制中的应用及发展[J]. 广东化工,2013,40(17):106-107.[3] 王伟. 连续重整汽油终馏点异常升高的原因分析及对策[J]. 炼油技术与工程, 2021,51(6):20-22.[4] 郑海,王永成. 二甲苯塔侧线气相抽出降低汽油馏分终馏点[J]. 石油炼制与化工, 2015,46(11):42-45.[5] 王彦龙. 降低连续重整汽油干点的技术改造及运行分析[J]. 化工管理, 2018 (18):135.[6] 罗家弼. 炼油技术常用数据手册[M]. 北京: 中国石化出版社,2016:70.

备注/Memo

备注/Memo:
-
更新日期/Last Update: 2023-05-10