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[1]陈君丽a,邵卫国b,余顺c,等.加氢裂化装置生产工业白油的模拟改造[J].石化技术与应用,2022,2:112-115.
　CHEN Jun-lia,SHAO Wei-guob,YU Shunc,et al.Simulated modification of industrial white oil production byhydrocracking unit[J].Petrochemical technology & application,2022,2:112-115.
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加氢裂化装置生产工业白油的模拟改造(PDF)

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

期数:
2022年2期
页码:
112-115
栏目:
出版日期:
2022-03-10

文章信息/Info

Title:
Simulated modification of industrial white oil production byhydrocracking unit
作者:
陈君丽a; 邵卫国b; 余顺c; 王娟a
中国石油独山子石化公司 a.研究院，b.安全环保质量处，c.炼油一部，新疆 克拉玛依 833699
Author(s):
CHEN Jun-lia;  SHAO Wei-guob;  YU Shunc;  WANG Juana
a. Research Institute， b. HSE Division， c. First Refinery Department， Dushanzi Petrochemical Company， PetroChina， Karamay 833699， China
关键词:
加氢裂化; 分馏塔; 工业白油; Aspen HYSYS流程模拟软件
Keywords:
hydrocracking;  fractionating tower;  industrial white oil;  Aspen HYSYS process simulation software
分类号:
TE 624.4+32
DOI:
DOI：10.19909/j.cnki.ISSN1009-0045.2022.02.0112
文献标识码:
B
摘要:
采用Aspen HYSYS流程模拟软件对某蜡油加氢裂化装置分馏塔进行流程模拟，分析了该装置生产5号工业白油的可行性，并提出相应的改造方案。结果表明：该装置重柴油产品中260~380 ℃馏分的芳烃质量分数、40 ℃运动黏度和闪点可满足5号工业白油指标要求；仅通过调整操作条件无法生产出合格的5号工业白油，但通过增设柴油蒸汽汽提塔，采用改变或不改变分馏塔馏出口的改造方案，均能生产出合格的5号工业白油。
Abstract:
The process flow of a fractionating tower in a hydrocracking unit was simulated by Aspen HYSYS process simulation software in order to analyze the feasibility of producing No.5 industrial white oil in hydrocracking unit and the corresponding revamp scheme was put forward. The results showed that the 260-380 ℃ fraction in heavy diesel oil from the unit has the suitable mass fraction of aromatics， kinematic viscosity at 40 ℃ and flash point that could meet the requirements of No. 5 industrial white oil， which showed that the No. 5 industrial white oil could be produced in this hydrocracking unit. The qualified No. 5 industrial white oil could not be produced by merely adjusting the process operating conditions， but could be produced by adding diesel stripper， adopting the revamp scheme of changing or not changing the distillation outlet.

参考文献/References

［1］ 曾文钦，方友，郑港西，等.蜡油加氢裂化装置生产工业白油的改造思路［J］.石油炼制与化工，2020，51（3）：22-26.
［2］ 熊伟庭.加氢裂化装置改造与生产5号工业白油的效果［J］.石油炼制与化工，2017，48（2）：16-20.
［3］ 陈君丽，托罗别克·苏勒太依，盛世.加氢裂化分馏塔的Aspen HYSYS 流程模拟优化［J］.石化技术与应用，2020，38（1）：36-38.

备注/Memo

备注/Memo:
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更新日期/Last Update: 2022-03-10