Numerical simulation on liquid-solid two-phase erosion characteristics of pipe bends with different bend angles

IF 3.7 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Chao Gao, Guiling Xu, Feihu Shen, Wenlong Du, Pengcheng Xu, Qi Zhang, Ping Lu
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Abstract

Pipeline transportation is a very common mode of transportation in the energy and chemical industries. Pipeline structure has an important effect on liquid-solid two-phase flow characteristics, which is vital to reduce the erosion wear of pipe bend. In this paper, an Eulerian-Lagrangian approach with liquid-solid two-phase coupling is performed to investigate the erosion characteristics of pipe bends with different bend angles of 60°, 90°, 120°, 135°, 150° and 165°. The computation domain is a pipeline segment comprising of two straight pipe sections of 250 mm in length, and a pipe bend with an inner diameter of 25 mm, a bend radius of 37.5 mm. The inlet boundary condition is set as “velocity-inlet”, and the material of the wall is aluminium with a density of 2702 kg/m3. The outlet boundary condition is set as “outflow”, The wall boundary condition is set as “reflect”, and the outlet boundary condition is set as “escape”. The influences of bend angle, solid particle size, solid-phase mass flow rate and liquid-phase inlet velocity on erosion rate distribution, velocity distribution, particle trajectory, and pressure distribution have been analyzed with CFD simulation combined with Discrete Phase Model (DPM). Results show that erosion mainly occurs on the external side of inner wall in the bend pipe section, with the 165° pipe bend exhibiting the lowest erosion rate and the erosion rate decreases with the increase of the bend angle. Meanwhile, the increase of solid particle size, solid-phase mass flow rate and liquid-phase inlet velocity will all aggravate the bend erosion. The flow field inside the pipe bend is significantly affected by the bend angle and the liquid-phase inlet velocity, while the particle characteristic parameters, including solid particle size and solid-phase mass flow rate have less effect. Furthermore, the flow field in the pipe bend shows the characteristics of secondary flow, with the increase of pipe bend angle, the high-pressure area on the inner outer wall of the pipe bend decreases gradually. The research results can provide some theoretical support for the optimal design of pipe bends in related industrial fields.
不同弯角管件液固两相冲蚀特性的数值模拟
管道运输是能源和化工行业中非常常见的一种运输方式。管道结构对液固两相流动特性有重要影响,对减少弯管的冲蚀磨损至关重要。本文采用考虑液固两相耦合的欧拉-拉格朗日方法,研究了60°、90°、120°、135°、150°和165°不同弯头的冲蚀特性。计算域为长度为250 mm的两段直管,弯道内径为25 mm,弯道半径为37.5 mm的管段。入口边界条件设为“速度-入口”,壁材为铝,密度为2702 kg/m3。出口边界条件设为“流出”,壁面边界条件设为“反射”,出口边界条件设为“逃逸”。采用CFD模拟和离散相模型(DPM)相结合的方法,分析了弯曲角、固体颗粒尺寸、固相质量流量和液相进口速度对侵蚀速率分布、速度分布、颗粒轨迹和压力分布的影响。结果表明:弯管段冲蚀主要发生在内壁外侧,165°弯管段冲蚀率最低,冲蚀率随弯管段角度的增大而减小;同时,固相颗粒尺寸的增大、固相质量流速率的增大和液相进口速度的增大都会加剧弯曲侵蚀。弯管内流场受弯角和液相进口速度的影响较大,而颗粒特性参数(固体粒径和固相质量流量)的影响较小。弯管内流场表现出二次流的特征,随着弯管角的增大,弯管内外壁的高压面积逐渐减小。研究结果可为相关工业领域的弯管优化设计提供一定的理论支持。
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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