石油化工设备技术 ›› 2019, Vol. 40 ›› Issue (4): 64-66.doi: 10.3969/j.issn.1006-8805.2019.04.014

• 节能 • 上一篇    

3.2 Mt/a连续重整装置混合进料换热器更换

孙秋荣   

  1. 武汉金中石化工程有限公司,湖北 武汉 430223
  • 收稿日期:2019-04-04 接受日期:2019-06-25 出版日期:2019-07-15 发布日期:2019-11-20
  • 作者简介:孙秋荣,男,1997年毕业于西安石油学院化学工程专业,工学学士,主要从事重整及芳烃工艺设计工作,高级工程师。Email:sunqr@whjpec.net

Replacement of Mixed Feed Heat Exchanger in 3.2Mt/a CCR Unit

Sun Qiurong   

  1. Wuhan Jinzhong Petrochemical Engineering Co., Ltd., Wuhan, Hubei, 430223
  • Received:2019-04-04 Accepted:2019-06-25 Online:2019-07-15 Published:2019-11-20

摘要: 介绍了某公司芳烃项目3.2 Mt/a连续重整装置混合进料换热器更换为缠绕管式换热器的运行情况。结合板壳式换热器和缠绕管式的结构特点,对更换前后运行参数进行对比分析发现,缠绕管式换热器在此处表现出热端温差低、管壳程压力降低、管壳程流体分布均匀等较优良的特性,消除了壳程出口压力的脉冲波动,实现了重整反应氢油比以及重整临氢系统压力降的大幅降低,节能降耗效果显著。

关键词: 连续重整装置, 板壳式换热器, 缠绕管式换热器, 更换

Abstract: This paper introduces the operation of a 3.2Mt/a continuous reforming unit with mixed feed heat exchanger replaced by spiral wounded heat exchanger in an aromatic hydrocarbon project of a company. Combined with the structural characteristics of plate heat exchanger and spiral wounded heat exchanger, the paper compares and analyzes the operating parameters before and after the replacement. And it is found that spiral wounded heat exchanger is superior in performance in such aspects as lower temperature difference at the hot end, reduced tube and shell pressure and uniform distribution of fluid at tube and shell side. This eliminates the impulse fluctuation of the shell outlet pressure and realizes a great reduction of the hydrogen-oil ratio of the reforming reaction and pressure drop of the reforming hydrogen system. And the energy saving and consumption reduction effect is remarkable.

Key words: continuous catalytic reforming unit/CCR unit, plate-shell heat exchanger, spiral wounded heat exchanger, replacement