欢迎访问过程工程学报, 今天是

过程工程学报 ›› 2023, Vol. 23 ›› Issue (4): 534-543.DOI: 10.12034/j.issn.1009-606X.222206

• 研究论文 • 上一篇    下一篇

原料射流对提升管内压降特性的影响

郑志航, 马郡男, 闫子涵*, 卢春喜   

  1. 中国石油大学(北京)重质油国家重点实验室,北京 102249
  • 收稿日期:2022-06-15 修回日期:2022-07-20 出版日期:2023-04-28 发布日期:2023-05-04
  • 通讯作者: 闫子涵 yanzihan2007@163.com
  • 作者简介:郑志航,硕士研究生,化学工程专业,E-mail: 2680197495@qq.com;通讯联系人,闫子涵,副教授,主要研究方向为多相流反应器开发、流态化技术、多相流传递与分离,E-mail: yanzihan2007@163.com
  • 基金资助:
    国家自然科学基金;国家重点研发计划

Effect of different types of feed injection on pressure drop characteristics in riser

Zhihang ZHENG,  Junnan MA,  Zihan YAN*,  Chunxi LU   

  1. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China
  • Received:2022-06-15 Revised:2022-07-20 Online:2023-04-28 Published:2023-05-04
  • Contact: Zi-Han YAN yanzihan2007@163.com

摘要: 通过大型冷模实验,采集了不同原料射流形式的提升管内总压降及预提升段、进料混合及充分发展段压降的动态数据,对比了斜向上射流和斜向下射流存在时提升管内各区域的压降特征,分析了不同操作条件的影响。结果表明,相同操作条件下,射流与多相流逆流接触提升管总压降及各部分压降大于射流与多相流并流接触提升管总压降及各部分压降。其他操作条件一定时,不同射流与多相流接触方式提升管总压降及各部分压降均随预提升气速增大而减小,随颗粒循环强度增加而增大。当射流速度增大时,射流与多相流并流接触提升管内总压降及各部分压降变化不明显;射流与多相流逆流接触提升管内预提升段压降有所增大,进料混合及充分发展段压降、提升管总压降显著增加。结合传统提升管压降模型及因次分析,建立了射流与多相流并流和射流与多相流逆流接触两种形式提升管内的进料混合及充分发展区压降模型,可供工程设计参考。

关键词: 提升管, 射流, 进料段, 压降

Abstract: Riser reactor is the core equipment of the catalytic cracking process. In an industrial riser reactor, the feed oil is usually injected by multiple high-speed nozzles to mix and react with catalyst particles. As an important monitoring data, the pressure drop in riser not only reflects the fluidization state but also determines the energy consumption of the process. However, most studies on the pressure drop in riser do not consider the effect of feed injection. The model to predict the pressure drop in the feed injection zone of riser needs to be improved. In this work, the pressure drop in riser under the effect of different types of feed injection is investigated through large-scale cold mold experiments. The dynamic data of both total pressure drop and pressure drop from different sections in riser are collected. Results under the influence of upward injection and downward injection are compared. Besides, the pressure drop characteristics of each section in the riser are analyzed, and the influence of different operating conditions is analyzed. Generally, both the total pressure drop and the pressure drop from each section of riser are larger when the catalysts contact with feed injection by countercurrent way. For both upward and downward jets, the total pressure drop and the pressure drop of each section in riser decrease with the increase of the pre-lift gas velocity, increase wiht the increase of solid flux. When the jet velocity increases, the total pressure drop and the pressure drop of each section in riser do not change significantly when the catalysts contact with feed injection by cocurrent way. On the contrary, for the countercurrent contact situation, the total pressure drop of riser and the pressure drops in the feed mixing and fully developed sections increase significantly. Combined with the traditional riser pressure drop model and dimensional analysis, pressure drop models for the feed mixing and fully developed sections in riser are established, which can be used as a reference for engineering design.

Key words: riser, jet, feed injection zone, pressure drop