Study of Erosion Behavior in Elbows Mounted in Series Using Computational Fluid Dynamics Method

2020 ◽  
Vol 142 (11) ◽  
Author(s):  
Zhenqiang Xie ◽  
Xuewen Cao ◽  
Juni Zhang ◽  
Xiaoyang Sun ◽  
Chenyang Fu ◽  
...  

Abstract To date, numerous studies using experimental methods or computational fluid dynamics (CFD) simulations to investigate erosion in elbows have been published. However, most of these studies focused on erosion caused by large particles flowing through a single elbow, whereas erosion due to small particles in elbows mounted in series is largely ignored. Studying erosion in elbows mounted in series is essential for improving the design of pipeline systems. In this paper, a CFD model is developed and validated against experimental data in the literature. The effects of both the connecting length (i.e., the distance between two elbows connected in series) and the elbow radius of curvature on erosion behavior were investigated using the verified model. In addition, the Dean number and Stokes number were used to investigate particle motion. The results show that erosion in the second elbow first decreases and then increases, as the connecting length increases, and the maximum erosion zone always occurs in the first elbow. However, when the number of elbows is increased to four, interestingly, the maximum erosion zone is located in the fourth elbow. The findings are valuable and provide guidance for designing novel pipeline systems that can mitigate erosion.

Author(s):  
D. Thiemsakul ◽  
◽  
R. Piemjaiswang ◽  
P. Piumsomboon ◽  
B. Chalermsinsuwan

Internally circulating fluidized bed reactor (ICFB) is the system with combining the function of reactor, cyclones and loop seal of a conventional circulating fluidized bed reactor (CFB) into a single reactor column. In this type of reactor, the reactor column is separated into two sections (riser and downer) by baffles and is linked together via connecting ports. This system is then considered as compact operation when comparing with the conventional CFB reactor. However, the simplicity of the ICFB reactor is trade-off with a gas leakage which takes place between the two sections through the connecting ports. In addition, the solid particle movement inside the system can cause the erosion on the inserting pipes which are used for heating or cooling this ICFB reactor column. In this study, the system hydrodynamics and erosion behavior inside ICFB reactor with inserting pipe were investigated by computational fluid dynamics (CFD) using two-dimensional Eulerian-Eulerian model. The adjusted Gidaspow drag model was applied to compute the interaction between the gas and solid particle phases. Then, the system hydrodynamics was obtained and the wall shear stress was calculated in the existent of the erosion at the surface region of the inserting pipes. The results from this simulation were used to design the inserting pipe arrangement inside this ICFB reactor.


2008 ◽  
Vol 47 (1) ◽  
pp. 192-200 ◽  
Author(s):  
Atilano Antônio Vegini ◽  
Henry França Meier ◽  
João Jaime Iess ◽  
Milton Mori

2020 ◽  
Vol 10 (1) ◽  
pp. 123-130
Author(s):  
Arnol Smith García Barbosa ◽  
Daniel Andres Antequera Cantillo ◽  
Juan Pablo Arango Restrepo ◽  
César Augusto Gómez Pérez ◽  
Jairo José Espinosa Oviedo

In this paper we present the design problem of helical tubular PhotoBioReactors (PBR) based on energy consumption minimization, using the radius of curvature for the cultivation of microalgae. Computational Fluid Dynamics (CFD) is used to design a configuration of the helical pipeline with minimum energy consumption. We determined how flow direction changes affect energy consumption. Additionally, it was found that the radius of curvature affects the pressure drop in the PBR’s pipe, so a cost function has been developed to solve an optimization problem seeking to obtain the optimum radius of curvature and a helical tubular PBR design with low pumping rates.


1996 ◽  
Vol 33 (9) ◽  
pp. 163-170 ◽  
Author(s):  
Virginia R. Stovin ◽  
Adrian J. Saul

Research was undertaken in order to identify possible methodologies for the prediction of sedimentation in storage chambers based on computational fluid dynamics (CFD). The Fluent CFD software was used to establish a numerical model of the flow field, on which further analysis was undertaken. Sedimentation was estimated from the simulated flow fields by two different methods. The first approach used the simulation to predict the bed shear stress distribution, with deposition being assumed for areas where the bed shear stress fell below a critical value (τcd). The value of τcd had previously been determined in the laboratory. Efficiency was then calculated as a function of the proportion of the chamber bed for which deposition had been predicted. The second method used the particle tracking facility in Fluent and efficiency was calculated from the proportion of particles that remained within the chamber. The results from the two techniques for efficiency are compared to data collected in a laboratory chamber. Three further simulations were then undertaken in order to investigate the influence of length to breadth ratio on chamber performance. The methodology presented here could be applied to complex geometries and full scale installations.


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