石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (11): 95-99.

• 设备及防腐 • 上一篇    下一篇

国产缠绕管式换热器在连续催化重整装置中的应用

孙宗伟,李泽,姚立松   

  1. 中国石化青岛炼油化工有限责任公司
  • 收稿日期:2025-06-09 修回日期:2025-07-25 出版日期:2025-11-12 发布日期:2025-10-24
  • 通讯作者: 孙宗伟 E-mail:sunzw2021.qdlh@sinopec.com

APPLICATION OF DOMESTIC SPIRAL TUBE HEAT EXCHANGER IN CONTINUOUS CATALYTIC REFORMING UNIT

  • Received:2025-06-09 Revised:2025-07-25 Online:2025-11-12 Published:2025-10-24

摘要: 以连续催化重整(简称重整)装置国产缠绕管式进料换热器为例,在相同负荷工况下,比较分析其与板壳式换热器的热端温差和管壳程总压差。结果表明,在相同负荷工况下,缠绕管式换热器比板壳式换热器热端温差降低35 ℃,管壳程总压差降低70 kPa,装置3.5 MPa蒸汽和燃料气消耗量明显减少,瓦斯消耗量节省约4355 t/a,节省费用约1290万元/a。根据缠绕管式换热器的应用结果,结合国内同类装置相似案例,进一步提出缠绕管式换热器长周期运转策略。

关键词: 连续催化重整装置, 缠绕管式换热器, 热端温差, 节能

Abstract: This article takes the domestically produced wound tube feed heat exchanger of the reforming unit as an example, and compares and analyzes its hot end temperature difference and total pressure drop on the tube shell side with the plate shell heat exchanger under the same load conditions. The results show that under the same load conditions, the temperature difference at the hot end of the coiled tube heat exchanger is reduced by 35 ℃ compared to the plate shell heat exchanger, the total pressure drop of the tube shell side is reduced by 70 kPa, the consumption of 3.5 MPa steam and fuel gas in the device is significantly reduced, and the gas consumption is saved by about 4355t/a, saving costs equivalent to 12.90 million yuan/a. Based on the successful application of coiled tube heat exchangers and similar cases of similar devices in China, a long-term operation strategy for coiled tube heat exchangers is further proposed.

Key words: continuous catalytic reforming unit, wrapped tube heat exchanger, hot end temperature difference, energy-saving