|本期目录/Table of Contents|

[1]代恩东,蒋秀军,陈国刚,等.常减压装置生产道路沥青的工艺流程模拟与优化[J].石化技术与应用,2023,6:465-470.
 DAI En-dong,JIANG Xiu-jun,CHEN Guo-gang,et al.Process simulation and optimization of producing road asphaltin atmospheric and vacuum distillation unit[J].Petrochemical technology & application,2023,6:465-470.
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常减压装置生产道路沥青的工艺流程模拟与优化(PDF)

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

期数:
2023年6期
页码:
465-470
栏目:
出版日期:
2023-11-10

文章信息/Info

Title:
Process simulation and optimization of producing road asphaltin atmospheric and vacuum distillation unit
文章编号:
1009-0045(2023)06-0465-06
作者:
代恩东1蒋秀军1陈国刚1毛玲娟12刘亭亭13*
1.浙江石油化工有限公司,浙江 舟山 316000;2.华北电力大学 能源动力与机械工程学院,北京 102208;3.浙江省绿色石化技术创新中心,浙江 宁波 315048
Author(s):
DAI En-dong1JIANG Xiu-jun1CHEN Guo-gang1MAO Ling-juan12LIU Ting-ting13
1.Zhejiang Petroleum & Chemical Co Ltd,Zhoushan 316000,China;2.College of Energy,Power and Mechanical Engineering,North China Electric Power University,Beijing 102208,China;3.Zhejiang Provincial Innovation Center of Green Petrochemical Technology(ZGPT),Ningbo 315048,China
关键词:
道路沥青常减压装置Petro-Sim流程模拟软件常压炉减压炉收率模拟优化
Keywords:
road asphaltatmospheric and vacuum distillation unitPetro-Sim process simulation softwareatmospheric furnacevacuum furnaceyieldsimulation optimization
分类号:
TE 626.8+61;TE 319
DOI:
DOI:10.19909/j.cnki.ISSN1009-0045.2023.06.0465
文献标识码:
B
摘要:
利用英国KBC公司开发的Petro-Sim流程模拟软件建立了常减压联合装置的机理模型,模拟优化了300万t/a常减压装置生产道路沥青的最佳生产操作条件。结果表明:通过提高常压塔塔底汽提蒸汽注入量,优化减压塔中段回流取热,可提高常减压装置的物料分离精度。经模拟优化后,当常压炉出口温度由358.0 ℃降低至347.0 ℃时,减压炉出口温度由375.0 ℃升高至398.0 ℃,使部分常压炉负荷转移至减压炉,不仅致使该常减压装置马瑞原油加工量由272.30 t/h提高至357.60 t/h,达到原设计加工量要求;而且产物中的石脑油、混合柴油、道路沥青产量依次增加了31.01%,51.21%,30.52%,尽管混合蜡油产量变化不大,但使该联合装置综合经济效益增收447.9万元/月。
Abstract:
The mechanism model of atmospheric and vacuum distillation unit was established by using Petro-Sim process simulation software developed by KBC Company in Britain. Then the optimum operating conditions of the combined 3.0 Mt/a atmospheric and vacuum distillation unit was simulated and optimized during producing road asphalt. The results showed that the material separation accuracy of this combined atmospheric and vacuum distillation unit could be improved by increasing the stripping steam injection capacity at the bottom of the atmospheric tower and optimizing the heat recovery by reflux in the middle section of the vacuum tower. After the simulation and optimization,when the outlet temperature of atmospheric furnace reduced from 358.0 ℃ to 347.0 ℃,the outlet temperature of vacuum furnace increased from 375.0 ℃ to 398.0 ℃,which transferred part of the processing load of atmospheric furnace to that of vacuum furnace. In this way,not only caused the actual processing capacity of Merey crude oil in this combined unit increase from 272.30 t/h to 357.60 t/h,which reached the original designed processing capacity requirements,but also the yield of naphtha,mixed diesel oil and road asphalt in the products increased by 31.01%,51.21% and 30.52% in turn,however the yield of mixed wax oil changed little,but the comprehensive economic benefit of this combined unit increased by 4.479 million yuan per month.

参考文献/References

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备注/Memo

备注/Memo:
浙江石油化工有限公司科研基金资助项目(项目编号:ZSH-RD-23-099)
更新日期/Last Update: 2023-11-10