石油炼制与化工 ›› 2019, Vol. 50 ›› Issue (5): 57-60.

• 加工工艺 • 上一篇    下一篇

糠醛精制抽余油生产环烷基橡胶增塑剂的工艺优化研究

张卉,蔡烈奎   

  1.  中海油炼油化工科学研究院
  • 收稿日期:2018-08-16 修回日期:2018-12-17 出版日期:2019-05-12 发布日期:2019-05-28
  • 通讯作者: 张卉 E-mail:zhanghui11@cnooc.com.cn
  • 基金资助:
    中海油环烷基减压馏分油生产低芳环烷基橡胶油的技术开发

STUDY OF PROCESS OPTIMIZATION FOR NAPHTHENIC RUBBER PLASTICIZER PRODUCTION FROM FURFURAL RAFFINATE OIL

  1.  
  • Received:2018-08-16 Revised:2018-12-17 Online:2019-05-12 Published:2019-05-28
  • Contact: Hui ZHANG E-mail:zhanghui11@cnooc.com.cn
  • Supported by:
     

摘要: 以绥中36-1减三线糠醛精制抽余油为原料,采用加氢处理+临氢降凝+补充精制三段加氢组合工艺,通过催化剂级配及工艺条件优化,制备环烷基橡胶增塑剂。结果表明:在加氢处理催化剂RL-1、临氢降凝催化剂SDD-800、加氢补充精制催化剂LN-5的体积空速分别为1.3,0.8,0.6 h-1,加氢处理及临氢降凝温度均为340 ℃、加氢补充精制温度为240 ℃时,可以得到满足HG/T 5085—2016《橡胶增塑剂环烷基矿物油》标准中产品N4010指标要求的环烷基橡胶增塑剂,收率超过90%。净利润较抽余油直接出售增加1 370 元/t,潜在经济效益显著。

关键词: 糠醛抽余油, 高压加氢, 催化剂级配, 环烷基橡胶增塑剂

Abstract: Furfural raffinate oil with low nitrogen and aromatics content is suitable to produce colorless and low aromatic rubber plasticizer. In this paper, we use raffinate oil from SZ36-1 No.3 vacuum cut as raw material to produce naphthenic rubber plasticizer by the combined process of hydrotreating (catalyst RL-1), hydrodewaxing (catalyst SDD-800) and hydrofinishing (catalyst LN-5). The LHSV of RL-1,SDD-800,LN-5 was 1.3,0.8,0.6 h-1,respectively. The reaction temperature of hydrotreating and hydrodewaxing were both 340℃ and the temperature of hydrofinishing was 240℃. The experimental results showed that naphthenic rubber plasticizer produced met the N4010 indexes of HG/T 5085-2016 “Rubber plasticizer-naphthene base mineral oil”, the yield of the product was over 90%. The net profit increases by 1, 370 RMB/t compared with the direct sale of the residual oil. The potential economic benefits are significant.

Key words: furfural raffinate oil, high pressure hydrotreating, catalyst gradation, naphthenic rubber plasticizer

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