石油化工设计 ›› 2021, Vol. 38 ›› Issue (4): 39-44.doi: 10.3969 /j.issn.1005-8168.2021.04.010

• 环保与安全 • 上一篇    下一篇

环氧乙烷装置多效蒸发系统的工程故障诊断及解决方法

邵璐   

  1. 中国石化工程建设有限公司,北京 100101
  • 收稿日期:2021-04-09 接受日期:2021-04-09 出版日期:2021-11-10 发布日期:2021-11-10
  • 通讯作者: 邵璐,shaol@sei.com.cn E-mail:shaol@sei.com.cn
  • 作者简介:邵璐,女,2000年毕业于贵州大学化学工程专业,硕士,现任公司专业副总监,正高级工程师。长期从事石油化工工程设计及管理工作。联系电话:010-84876839;E-mail: shaol@sei.com.cn

Engineering Fault Diagnosis of Multi-effect Evaporation System in Ethylene Oxide Plant and the Solutions

Shao Lu   

  1. SINOPEC Engineering Incorporation, Beijing, 100101
  • Received:2021-04-09 Accepted:2021-04-09 Online:2021-11-10 Published:2021-11-10
  • Contact: Shao Lu,shaol@sei.com.cn E-mail:shaol@sei.com.cn

摘要: 多效蒸发是工业生产中常用的节能工艺,但在实际工程设计中,各效间的有效传热温差分配与控制问题却鲜有人涉及,实际操作中一般各效温差通过自平衡实现,往往偏离设计值较多,导致操作可控性差,容易出现压力波动、液泛或雾沫夹带等问题。以某环氧乙烷装置中开车运行中出现的问题为例,本文分别从工艺设计和控制运行两方面分析了操作压力偏离设计的原因及影响,提出了解决措施,优化了设计,并在实际改造中得以应用,大大提高了装置运行的稳定性

关键词: 多效蒸发, 乙二醇, 环氧乙烷, COD超标

Abstract: Multi-effect evaporation is a commonly used energy-saving process in industrial production. However, in actual engineering design, few people have proposed the exact design method for the effective heat transfer temperature difference distribution of each effect. In practice, the temperature difference of each effect is generally realized through self balance. Accordingly, the operation controllability in production is poor, and problems such as pressure fluctuation, liquid flooding or mist entrainment are easy to occur. This paper takes the problems occurred during the start-up of an ethylene oxide plant as an example, analyzes the reasons and effect of the operating pressure deviation from design value from two aspects of process design and control operation, gives solutions to the problems and optimizes the design, greatly improving the operation stability of the plant.

Key words: multiple effect evaporation, ethylene glycol, ethylene oxide, COD exceeds the standard