石油化工设备技术 ›› 2022, Vol. 43 ›› Issue (5): 28-34.doi: 10.3969/j.issn.1006-8805.2022.05.006

• 工业炉 • 上一篇    

加热炉出口管线内气液流场的数值模拟研究

孟振亮   

  1. 中国石化工程建设有限公司,北京 100101
  • 收稿日期:2022-07-10 接受日期:2022-08-30 出版日期:2022-09-15 发布日期:2022-11-16
  • 作者简介:孟振亮,男,2018年毕业于中国石油大学(北京)动力工程及工程热物理专业,工学博士,主要从事石油化工设备的设计、研发工作,工程师,已发表论文4篇。

Numerical Simulation of Gas-liquid Flow in the Outlet Pipeline of Heating Furnace

Meng Zhenliang   

  1. SINOPEC Engineering Incorporation, Beijing, 100101
  • Received:2022-07-10 Accepted:2022-08-30 Online:2022-09-15 Published:2022-11-16

摘要: 采用欧拉-欧拉模型对加氢精制装置加热炉出口管段内的气-液两相流进行了三维CFD(Computational Fluid Dynamics)数值模拟,重点研究了现有管线结构下气-液两相的浓度场及速度场分布并提出了管线布置优化方案。研究结果表明:现有管线布置方案由于气、液惯性力不同,两相流体经过多个弯头在三维空间连续改变流动方向,在管线中形成了螺旋流动;通过对布置方案进行优化,部分消除了沿径向旋转的驱动力,减少了螺旋流。研究结果可为加热炉出口管线布置方案优化提供指导。

关键词: 加热炉, 出口管线, 气-液两相流, 数值模拟

Abstract: Eulerian-Eulerian model was applied to conduct 3D CFD (Computational Fluid Dynamics) numerical simulation of the gas-liquid flow in the outlet pipeline of the heating furnace in hydrorefining unit. The distribution of the concentration field and velocity field of gas-liquid phase under the existing pipeline structure were studied and the optimization of the pipeline arrangement was proposed. The research results indicate that due to the different inertia forces of gas and liquid, a spiral flow was formed in the pipeline in the existing pipeline arrangement scheme after the gas-liquid flow changing multiple directions in the 3D space; by optimizing the arrangement scheme, the driving force along the radial rotationwas partially eliminated and the spiral flow of the fluid was reduced. The research results can provide guidance for the optimization of the arrangement scheme for the outlet pipeline of heating furnace.

Key words: heating furnace, outlet pipeline, gas-liquid two-phase flow, numerical simulation