[1]汪进,丁丽颖,韩雪,等.轻汽油醚化装置预加氢单元轻重汽油分离系统的模拟优化[J].石化技术与应用,2023,1:48-51.
WANG Jin,DING Li-ying,HAN Xue,et al.Simulation and optimization of gasoline separation system in prehydrogenation unit of light gasoline etherification unit[J].Petrochemical technology & application,2023,1:48-51.
点击复制
轻汽油醚化装置预加氢单元轻重汽油分离系统的模拟优化(PDF)
《石化技术与应用》[ISSN:1009-0046/CN:62-1138/TQ]
- 期数:
-
2023年1期
- 页码:
-
48-51
- 栏目:
-
- 出版日期:
-
2023-01-10
文章信息/Info
- Title:
-
Simulation and optimization of gasoline separation system in prehydrogenation unit of light gasoline etherification unit
- 文章编号:
-
1009-0045(2023)01-0048-04
- 作者:
-
汪进; 丁丽颖; 韩雪; 费翔; 周婷; 陈红
-
中海油石化工程有限公司 工艺系统室,山东 青岛266000
- Author(s):
-
WANG Jin; DING Li-ying; HAN Xue; FEI Xiang; ZHOU Ting; CHEN Hong
-
Process System Department of Petrochemical Engineering Co Ltd,CNOOC,Qingdao 266000,China
-
- 关键词:
-
轻汽油; 醚化; 加氢; 分离; 模拟; 优化
- Keywords:
-
light gasoline; etherification; hydrogenation; separation; simulation; optimization
- 分类号:
-
TE 624.41
- DOI:
-
DOI:10.19909/j.cnki.ISSN1009-0045.2023.01.0048
- 文献标识码:
-
B
- 摘要:
-
利用Aspen HYSYS软件对轻汽油醚化装置预加氢单元的轻重汽油分离系统进行模拟计算,从操作条件、产品质量、设备情况、公用工程消耗等方面对3种分离方案进行对比。结果表明:汽提塔和分馏塔方案流程较复杂,产品质量较优,设备投资较大,但能耗较小;分馏塔-塔顶产出产品方案,流程简单,设备投资和能耗均较小,但轻汽油产品初馏点较低,易对下游醚化单元操作造成不利影响;分馏塔-侧线产出产品方案,产品质量最优,但设备投资和能耗较大。
- Abstract:
-
The gasoline separation system in a prehydrogenation unit of a light gasoline etherification unit was simulated and calculated by Aspen HYSYS software. Three common separation schemes were compared in terms of operating conditions, product quality, equipment conditions and general utility consumption. The results showed that the stripper and fractionator scheme′s process was relatively complex, but with better product quality, higher equipment investment,but less energy consumption. The scheme in which products comes out from the top of the fractionation tower had a simple process, small equipment investment and energy consumption, but the initial distillate point of light gasoline products was low, which was easy to cause adverse effects on the downstream etherification unit operation. The solution of product output from fractionating tower-side line output had the best product quality, but the equipment investment and energy consumption were high.
参考文献/References
[1] 郭锐.汽油醚化工艺探讨及关键控制点[J].石油石化物资采购,2022(10):19-21.[2] 张斌,彭蓉,韩洋,等.催化裂化轻汽油选择性加氢除二烯烃工艺研究[J].上海化工,2014(9):4-8.[3] 刘蕾,姚文君,赵新红,等.催化裂化汽油清洁化技术研究进展[J].炼油与化工,2021,32(4):1-5.[4] 胡洋.汽油加氢工艺技术研究[J].石化技术,2020,27(7):75.[5] 王廷海,李文涛,常晓昕,等.催化裂化汽油清洁化技术研究开发进展[J].化工进展,2019,38(1):196-207.[6] 陆德才,金月昶,王铁刚,等.催化汽油预加氢技术现状及进展[J].当代化工,2012,41(9):884-887.[7] 许长辉.GARDES 技术在汽油加氢脱硫装置的工业应用[J].石油炼制与化工,2015,46(1):62-67.[8] 王伟,牛世坤,陈光.催化裂化汽油轻重分离点的优化与选择[J].当代化工,2020,49(6):1229-1232.
更新日期/Last Update:
2023-01-10