石油化工设计 ›› 2023, Vol. 40 ›› Issue (1): 52-55.doi: 10.3969 /j.issn.1005 -8168.2023.01.013

• 工艺优化 • 上一篇    

环氧乙烷精制塔超压工况泄放动态模拟

张继敏   

  1. 中国石化工程建设有限公司,北京 100101
  • 收稿日期:2022-03-04 接受日期:2022-03-04 出版日期:2023-02-25 发布日期:2023-03-07
  • 通讯作者: 张继敏,zhangjimin@sei.com.cn E-mail:zhangjimin@sei.com.cn
  • 作者简介:张继敏,男,2015年毕业于浙江大学化学工程专业,工学硕士,工程师,主要从事石油化工设计工作。联系电话:010-84876825;E-mail: zhangjimin@sei.com.cn

Dynamic Simulation of Overpressure Relief in Ethylene Oxide Purification Column

Zhang Jimin   

  1. SINOPEC Engineering Incorporation,Beijing,100101
  • Received:2022-03-04 Accepted:2022-03-04 Online:2023-02-25 Published:2023-03-07
  • Contact: Zhang Jimin,zhangjimin@sei.com.cn E-mail:zhangjimin@sei.com.cn

摘要: 针对某EO/EG装置中环氧乙烷精制塔系统,采用Aspen HYSYS软件对环氧乙烷精制塔系统冷却水中断、停电工况、调节阀关闭等超压工况进行动态模拟,获得不同超压工况下塔内压力、温度、介质组成、再沸器热负荷等操作参数的变化情况和安全阀峰值泄放量。以冷凝器冷却水故障工况为例,动态模拟的安全阀峰值排量215 t/h明显小于传统估算方法的313 t/h。动态模拟能够为该系统的安全阀选型、安全阀排放扩散计算以及排放气处理方案等提供设计优化的依据

关键词: 环氧乙烷精制塔, 动态模拟, 超压工况, 安全阀峰值泄放量

Abstract: For the ethylene oxide purification column system in an EO/EG plant, Aspen HYSYS was used to dynamically simulate the overpressure scenarios such as the failure of cooling water, power and control valve, so as to obtain the peak relief capacity of safety valve and the changes in operating parameters including tower pressure, temperature, medium composition and reboiler heat duty under different overpressure scenarios. Taking the cooling water failure scenario as an example, the peak discharge flowrate of safety valve from the dynamic simulation is 215 t/h, significantly lower than 313 t/h from the traditional estimation method. Dynamic simulation can provide basis for the design optimization of safety valve selection, safety valve discharge diffusion calculation and discharge gas treatment scheme.

Key words: EO purification column, dynamic simulation, overpressure scenario, peak relief capacity of safety valve