石油炼制与化工

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环己酮装置废碱液分离技术的工业应用

周萍 白志山 汪华林 杨强   

  1. 华东理工大学,化工机械研究所,上海 华东理工大学 华东理工大学
  • 收稿日期:2007-09-27 修回日期:1900-01-01 出版日期:2008-06-12 发布日期:2008-06-12
  • 通讯作者: 周萍

COMMERCIAL APPLICATION OF THE SEPARATION TECHNOLOGY FOR WASTE LYE OF CYCLOHEXANONE PRODUCTION UNIT

ZHOU Ping   

  • Received:2007-09-27 Revised:1900-01-01 Online:2008-06-12 Published:2008-06-12
  • Contact: ZHOU Ping

摘要: 为解决环己烷氧化法制备环己酮中氧化液废碱的分离问题,提出了将重力沉降技术、旋流分离技术和聚结分离技术依次串联组合的梯度分离技术,同时采用较为先进的两段逆流碱洗工艺,实现水的循环利用。该技术在巴陵石油化工有限责任公司80kt/a环己酮生产装置上的应用结果表明,当一级碱洗分离器进口Na+含量在2.92%~3.20%,经过碱洗分离系统处理后,聚结器出口有机相中Na+的质量浓度由改造前的6 mg/L以上降低为3mg/L以下,聚结器出口有机相中水含量由改造前的0.1%~0.2%降低为0.05%左右。环己酮生产工艺中烷蒸馏塔工作周期由改造前的平均2个月延长至9个月以上,实现整套装置长周期稳定运转。同时,降低了生产成本,减少了环境污染。

关键词: 环己酮, 碱洗, 分离, 工业规模

Abstract: In order to solve the waste lye separation problem of preparing cyclohexanone from cyclohexane, a gradient separation technique based on gravity sedimentation, hydrocyclone and coalescence techniques in series was proposed. Besides, a two stage countercurrent process of alkali wash was applied for the recycling water. This technology was adopted in the 80Kt/a cyclohexanone production unit of Baling Petrochemical Company successfully. The commercial application results showed that when the Na+ content of the 1st stage alkali wash separator inlet was in the range of 2.92%~3.20%, after treatment in the organic phase the contents of Na+ and water dropped form more than 6 mg/L (prior revamping) to less than 3 mg/L, and from 0.1%~0.2% (prior revamping) to 0.05%, respectively. The running length of alkane distillation column was prolonged from average 2 months to more than 9 months. Furthermore, the production cost was reduced, as well as less pollution.

Key words: cyclohexanone, caustic washing, separation, full scale