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过程工程学报 ›› 2024, Vol. 24 ›› Issue (6): 692-704.DOI: 10.12034/j.issn.1009-606X.223294

• 研究论文 • 上一篇    下一篇

低管径比固定床反应器床层特性及流动传热模拟

莫畏难, 苏有勇*, 朱冬冬   

  1. 昆明理工大学现代农业工程学院,云南 昆明 650500
  • 收稿日期:2023-10-30 修回日期:2023-12-26 出版日期:2024-06-28 发布日期:2024-06-26
  • 通讯作者: 苏有勇 497611561@qq.com

Bed characterization and flow heat transfer simulation of fixed bed reactor with low tube to particle diameter ratios

Weinan MO,  Youyong SU*,  Dongdong ZHU   

  1. School of Modern Agricultural Engineering, Kunming University of Science and Technology, Kunming, Yunnan 650500, China
  • Received:2023-10-30 Revised:2023-12-26 Online:2024-06-28 Published:2024-06-26
  • Contact: su youyong 497611561@qq.com

摘要: 管式固定床常用于高温催化裂解工艺,探究低管径比固定床结构特性和高温下流动传热规律,可以为优化固定床高温催化裂解工艺提供参考。针对粒子解析法中离散元DEM方法对颗粒描述不准确和网格划分困难的问题,采用基于刚体动力学的blender生成床层堆积模型,并提出了新的接触点处理方法。该方法不改变颗粒和床层形状参数,适用于各种形状颗粒,减小了模型接触处理难度。生成了三种反应管内径与柱状颗粒的等比表面积球当量直径之比(管径比D/dp)的圆柱状颗粒床层和一种球状颗粒床层,探究了管径比和颗粒形状对床层结构和流动传热特性的影响。结果表明,床层总体空隙率随着管径比增大而减小,颗粒堆积呈圈层分布,径向空隙率和轴向平均速度的径向分布曲线高度一致,压降与Eisfeld修正式基本吻合。此外,床层流场分布与床层结构高度相关,流道空隙的大小会直接影响沟流现象的产生,进一步影响其温度场分布和传热。球状颗粒床层有更均匀的温度场分布,但传热弱于圆柱状颗粒床层。

关键词: 固定床反应器, 接触点处理方法, 压降, 流动传热, 数值模拟

Abstract: Tubular fixed beds are widely used in high-temperature catalytic cracking processes. Investigating the structural characteristics of fixed beds with low tube to particle diameter ratios and the flow heat transfer laws at high temperatures can provide valuable insights for optimizing the fixed bed high-temperature catalytic cracking process. To address the issues of inaccurate particle description in the discrete element method and difficulty in mesh delineation in the particle resolution method, a new contact point method is proposed. This method does not alter the particle and bed size and shape parameters, adapts to various particle shapes, and significantly reduces the difficulty of model contact processing. Three cylindrical particle beds with different ratios of the inner diameter of the reaction tube to the equivalent diameter of spheres of equal specific surface area of the cylindrical particles (tube-diameter ratio D/dp) and one spherical particle bed are generated to investigate the effects of tube size ratio and particle shape on bed structure and flow heat transfer characteristics. The results show that the overall void ratio of the bed layer decreases with increasing tube to particle diameter ratio, the particle stacking is distributed in circles, and the radial distribution curves of radial void ratio and axial mean velocity are highly consistent. Additionally, the pressure drop is generally consistent with Eisfeld modified equation. Furthermore, the bed flow field distribution is highly correlated with the bed structure, and the size of the flow channel voids directly affects the generation of channel flow phenomena, which further impacts its temperature field distribution and heat transfer performance. The sphere particle bed exhibits a more uniform temperature field distribution, but its heat transfer performance is not as good as that of the cylind particle bed.

Key words: Fixed-bed reactor, Contact point method, Pressure drop, Flow heat transfer, Numerical simulation