|本期目录/Table of Contents|

[1]赵晶晶,董海军,马琼丽.高密度聚乙烯装置流化床运行周期短的原因分析及对策[J].石化技术与应用,2024,3:212-215.
　ZHAO Jing-jing,DONG Hai-jun,MA Qiong-li.Cause analysis and countermeasures of short operating cycle of fluidized bed in high density polyethylene plant[J].Petrochemical technology & application,2024,3:212-215.
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高密度聚乙烯装置流化床运行周期短的原因分析及对策(PDF)

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

期数:
2024年3期
页码:
212-215
栏目:
出版日期:
2024-05-10

文章信息/Info

Title:
Cause analysis and countermeasures of short operating cycle of fluidized bed in high density polyethylene plant
文章编号:
1009-0045（2024）03-0212-04
作者:
赵晶晶; 董海军; 马琼丽
中国石油兰州石化公司 榆林化工有限公司，陕西 榆林 719000
Author(s):
ZHAO Jing-jing; DONG Hai-jun; MA Qiong-li
Yulin Chemical Co Ltd，Lanzhou Petrochemical Company，PetroChina，Yulin 719000，China
关键词:
聚乙烯; 高密度聚乙烯; 流化床; 运行周期; 分布板; 离心机; 循环风机; 床层压差
Keywords:
polyethylene; high density polyethylene; fluidized bed; operating cycle; distribution plate; centrifuge; circulating fan; bed pressure difference
分类号:
TQ 325.1+2
DOI:
DOI：10.19909/j.cnki.ISSN1009-0045.2024.03.0212
文献标识码:
B
摘要:
对中国石油兰州石化公司榆林化工有限公司40万t/a高密度聚乙烯装置流化床出现分布板筛孔堵塞、通道粉料堆积、加热板粉料挂壁严重等问题造成流化床运行周期短的原因进行了分析，并采取了相应的优化措施。结果表明：上述问题是由聚合反应系统产生块状树脂，流化床进、出料流量波动大，通道设计缺陷以及循环N2风机设计功率偏小等因素引起的；通过采取优化聚合反应、离心机、流化床等系统操作，消除气力输送系统运行故障等措施，将乙烯进料量由18~45 t/h提高到52 t/h，流化床1腔床层压差由5.5 kPa降低至4.5 kPa，流化床运行周期由90 d延长至288 d。
Abstract:
The reasons for the short operating cycle of the fluidized bed in the 4×105 t/a high density polyethylene plant of Yulin Chemical Co Ltd of Lanzhou Petrochemical Company of PetroChina which were caused by the problems such as the blockages of the distribution plate sieve holes， the accumulation of channel powder， and the powder severely hanging on the heating plate were analyzed， and the corresponding optimization measures were taken. The results showed that the above problems were caused by the factors such as the blocky resin produced by the polymerization reaction system， the large fluctuations of the inlet and outlet flow of the fluidized bed， the defects of the channel design， and the small design power of the circulating N2 fans. By optimizing the operation of the polymerization reaction， centrifuge， fluidized bed and other systems， and eliminating the operation faults of the pneumatic conveying system， the ethylene inlet amount was increased from 18-45 t/h to 52 t/h， the bed pressure difference of fluidized bed 1 chamber was reduced from 5.5 kPa to 4.5 kPa， and the operation cycle of fluidized bed was extended from 90 d to 288 d.

参考文献/References

［1］ 李兵.高密度聚乙烯技术进展［J］.当代化工，2006，35（5）：322-325.［2］ 葛传龙.高密度聚乙烯装置流化床干燥器运行周期短的原因分析及建议［J］.当代化工，2020，49（9）：2075-2078.［3］ 王勇，石一刚，王婷婷，等.Unipol工艺聚乙烯装置反应器分布板堵塞原因分析［J］.当代化工，2018，47（9）：1969-1971.［4］ 翟畅，胡利博.流化床运行效果优化研究［J］.当代化工，2021，50（12）：2979-2982.［5］ 周志宇.聚乙烯生产技术问答［M］.北京：化学工业出版社，2014：27-28.

备注/Memo

备注/Memo:
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更新日期/Last Update: 2024-05-10