炼油技术与工程 ›› 2024, Vol. 54 ›› Issue (3): 28-31.

• 机械设备 • 上一篇    下一篇

汽油加氢装置反应器泡罩式分配器气相分配特性研究

陈超, 陈强   

  1. 中石化广州工程有限公司; 中石化炼化工程(集团)股份有限公司洛阳技术研发中心
  • 收稿日期:2023-10-01 出版日期:2024-03-15 发布日期:2024-03-21
  • 作者简介:陈超,高级工程师,毕业于天津大学化学工艺专业,主要从事加氢装置工艺设计工作。联系电话:020-22192845,E-mail:chenchao.lpec@sinopec.com。

Research on gas phase distribution characteristics of the bubble-cap distributor of the reactor in gasoline hydrogenation unit

Chen Chao, Chen Qiang   

  1. SINOPEC Guangzhou Engineering Co., Ltd.; Luoyang R&D Center of Technology of SINOPEC Engineering (Group) Co., Ltd.
  • Received:2023-10-01 Online:2024-03-15 Published:2024-03-21

摘要:

分析了汽油二段气相加氢过程中广泛使用的泡罩式分配器的主要特点和工作原理,并对泡罩式分配器分别进行了单体试验研究和组合试验研究,以分布不均匀系数和压力降为性能评价指标,探究其气相分配特性。试验结果表明:泡罩式分配器的分布效果不受风量的影响,增大风量不能提升纯气相分布效果,反而增大了流动阻力,使得压力降变大;并且由于结构原因,导致气相从中心管流出后都基本集中在中心管正下方,扩散范围较小,没有在整体匹配上形成较好的融合。从最优化和系统节能角度分析,泡罩结构的分配器作为气相分配器并不是最佳结构,因此在不影响分配特性的情况下,新型气相分配器应该采用非泡罩结构,进而大大降低气相流动阻力,并且在设计气相加氢分配器时,不仅要考虑分配器的单体分布性能,还要考虑相邻分配器之间的相互影响,尽可能扩大单体分配面积的同时均化组合流场,以提高内件运行过程中的安全稳定性。

关键词: 汽油加氢装置, 反应器, 泡罩式, 分配器, 气相分配, 不均匀度, 分配器压力降

Abstract:

In this paper, the main characteristics and principles of the bubble-cap distributor which widely used in the second stage gas phase hydrogenation of gasoline are analyzed. At the same time, the single test and combination test of the bubble-cap distributor are carried out respectively. The uneven distribution coefficient and pressure drop are used as performance evaluation indexes to explore its gas phase distribution characteristics. The experimental results show that the distribution performance of bubble-cap distributor is not affected by the air volume. Increasing the air flow rate can not improve the gas phase distribution performance, but increases the flow resistance and the pressure drop. And due to structural reasons, the gas phase after flowing out of the central tube is basically concentrated under the central tube, with a small diffusion range, and the cooperation is not formed. According to the performance and energy saving analysis, the bubble cap structure distributor is not the best structure as a gas phase distributor. Therefore, without affecting the distribution characteristics, the new gas phase distributor should adopt a non-bubble cap structure, thus greatly reducing the gas phase flow resistance. In addition, the distribution performance of the unit and the interaction between the adjacent units should be considered, and the distribution area should be expanded as much as possible. The homogenized combined flow field can improve the safety and stability of the internals during operation.

Key words: gasoline hydrogenation unit, reactor, bubble-cap, distributor, gas phase distribution, unevenness, pressure drop of distributor