辽宁石油化工大学学报

辽宁石油化工大学学报 ›› 2011, Vol. 31 ›› Issue (3): 12-15.DOI: 10.3696/j.issn.1672-6952.2011.03.004

• 石油化工 • 上一篇    下一篇

加氢尾油催化降凝生产润滑油基础油

张秋萍,石薇薇,董建军,赵德智*   

  1. 辽宁石油化工大学石油化工学院,辽宁抚顺113001
  • 收稿日期:2011-03-20 出版日期:2011-09-25 发布日期:2017-07-05
  • 作者简介:张秋萍(1986-),女,辽宁沈阳市,在读硕士。

 
Lube Base Oil produced by Catalytic Dewaxing From Hydrocracking Tail Oil

ZHANG Qiu-ping，SHI Wei-wei，DONG Jian-jun，ZHAO De-zhi*   

  1. School of Petrochemical Technology，Liaoning Shihua University，Fushun Liaoning 113001，P.R.China
  • Received:2011-03-20 Published:2011-09-25 Online:2017-07-05

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摘要： 以茂名石化加氢裂化尾油为原料,使用NKC-7型催化降凝催化剂,在固定床催化降凝装置上进行
实验。在温度为340~400℃、空速为1~8h-1的条件下,考察了反应温度、空速对产品分布、凝点、收率的影响。结
果表明:当温度为380℃、空速为2h-1时,得到较好的产品分布,润滑油基础油的凝点为-24℃,收率为61.4%。

关键词: 催化降凝 ,  ,  , 加氢尾油 ,  ,  , 催化剂 , 润滑油基础油

Abstract:  

Lube base oil were produced by catalytic dewaxing from hydrocracking tail oil of the Mao Ming Petrochemical Corporation in fixed catalytic bed reactor using NKC-7 as the dewaxing catalyst. The effects of reaction temperature (340～400 ℃) and space velocity( 1～8 h-1) on the product distribution, solidifying point and liquid yield were studied. The results show that good product distribution and higher yield of lube base oil (61.4 % ) can be obtained at 380 ℃ and a space velocity of 2 h-1, the solidifying point of lube base oil can reach -24 ℃.

Key words: Catalytic dewaxing   ,  Hydrocracking tail oil   ,  Catalyst   ,  ,  Lube base oil

引用本文

张秋萍,石薇薇,董建军,赵德智. 加氢尾油催化降凝生产润滑油基础油[J]. 辽宁石油化工大学学报, 2011, 31(3): 12-15.

ZHANG Qiu-ping,SHI Wei-wei,DONG Jian-jun,ZHAO De-zhi.  

Lube Base Oil produced by Catalytic Dewaxing From Hydrocracking Tail Oil
[J]. Journal of Liaoning Petrochemical University, 2011, 31(3): 12-15.

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链接本文: http://journal.lnpu.edu.cn/CN/10.3696/j.issn.1672-6952.2011.03.004

               http://journal.lnpu.edu.cn/CN/Y2011/V31/I3/12



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