石油炼制与化工 ›› 2026, Vol. 57 ›› Issue (6): 65-71.

• 加工工艺 • 上一篇    下一篇

生产60号工业己烷溶剂油项目改造及效果

饶勇建,黎小龙,蒋敏,杨正炳,周济群,龚传波   

  1. 中国石油独山子石化分公司
  • 收稿日期:2025-10-20 修回日期:2026-02-05 出版日期:2026-06-12 发布日期:2026-05-22
  • 通讯作者: 饶勇建 E-mail:lyc_ryj@petrochina.com.cn

TRANSFORMATION AND EFFECT OF No.60 INDUSTRIAL HEXANE SOLVENT OIL PROJECT

  • Received:2025-10-20 Revised:2026-02-05 Online:2026-06-12 Published:2026-05-22

摘要: 某石化公司芳烃抽提装置于1995年投产,原设计未考虑己烷溶剂油的生产。2001年5月改造后能够生产企业内部互供料标准的己烷溶剂油。为了进一步提高己烷溶剂油质量,提出了60号工业己烷溶剂油项目改造方案,通过对几种改造方案的比选,确定了将溶剂油分离塔6号溶剂油抽出线下移至原120号溶剂油抽出线位置,增加己烷组分与6号溶剂油抽出线之间的填料段,提高两者分离效果。同时通过简单调整流程利旧原有机泵,减少改造成本。2024年8月实施后,生产出符合GB/T 17602—2018要求的60号工业己烷溶剂油,同时提高了60号工业己烷溶剂油的产量。

关键词: 芳烃抽余油加氢, 60号工业己烷溶剂油, 方案比选

Abstract: The aromatics extraction unit of a petrochemical company was put into operation in 1995, and the original design did not take into account the production of hexane solvent oil.After a transformation in May 2001, it became capable of producing hexane solvent oil that could meet the internal supply standards of the enterprise. To further improve the quality of hexane solvent oil, a transformation plan for the No.60 industrial hexane solvent oil project was proposed. Through the selection of several transformation plans, it was decided to move the No.6 solvent extraction line of the solvent oil separation tower downward to the original No.120 solvent extraction line position and add a packing section between the hexane component and the No.6 solvent oil extraction to enhance their separation effect. At the same time, by simply adjusting the process and reusing the existing pump, the transformation cost was reduced. After implementation in August 2024, No.60 industrial hexane solvent oil that can meet the GB/T 17602—2018 standard was produced, and the output of No.60 industrial hexane solvent oil was also increased.

Key words: aromatics raffinate hydrogenation, No.60 industrial hexane solvent oil, transformation plan selection