Numerical and experimental study of finned tube erosion protection methods

Abstract Erosion of tubes by coal particles or coal ash impingement has caused serious problems to many pulverized coal energy conversion systems (such as the circulating fluidized bed combustion system). It is important to study erosion protection methods for tubes undergoing erosion. In this paper we present the results of numerical and experimental investigation of a new type of erosion-protection method: the finned tube erosion protection method. An experimental investigation of finned tube erosion processes was made by placing erosionprone wax cylinders with fins in a bench-scale cold flow circulating fluidized bed to simulate the long-term erosion effect. A numerical study was conducted for the flow of a dilute particle-laden gas moving past a finned tube undergoing erosion. An orthogonal curvilinear coordinate system was used to calculate turbulent flow around the finned tube. The calculation of particle trajectories took into account the effect of the turbulence with a stochastic particle dispersion model. The results from this study show that the finned tube is a simple and efficient erosion protection method in most industrial two-phase systems where erosion occurs. The fin relative height, the fin number and the angle between two adjacent fins are three important parameters which affect finned tube erosion protection abilities.

[1]  J. A. Laitone,et al.  Aerodynamic effects in the erosion process , 1979 .

[2]  I. Finnie Some observations on the erosion of ductile metals , 1972 .

[3]  B. Launder,et al.  THE NUMERICAL COMPUTATION OF TURBULENT FLOW , 1974 .

[4]  K. Cen,et al.  Numerical modeling and experimental study of particle-laden coaxial jets , 1989 .

[5]  R. Clift,et al.  Bubbles, Drops, and Particles , 1978 .

[6]  B. Launder,et al.  Mathematical Models of turbulence , 1972 .

[7]  K. A. Antonopoulos Prediction of flow and heat transfer in rod bundles , 1979 .

[8]  W. Tabakoff,et al.  Erosion Prediction in Turbomachinery Resulting from Environmental Solid Particles , 1975 .

[9]  Cen Ke-fa,et al.  Numerical simulation of tube erosion by particle impaction , 1991 .

[10]  J. A. C. Humphrey,et al.  Numerical calculation of particle‐laden gas flows past tubes , 1989 .

[11]  J. Laitone A Numerical Solution for Gas-Particle Flows at High Reynolds Numbers , 1981 .

[12]  W. Tabakoff,et al.  Erosion study of different materials affected by coal ash particles , 1979 .

[13]  S. Patankar Numerical Heat Transfer and Fluid Flow , 2018, Lecture Notes in Mechanical Engineering.

[14]  E. Raask Tube erosion by ash impaction , 1969 .

[15]  A. Gosman,et al.  Aspects of computer simulation of liquid-fuelled combustors , 1981 .

[16]  A. Gosman,et al.  Aspects of Computer Simulation of Liquid-Fueled Combustors , 1983 .

[17]  G. L. Sheldon,et al.  An investigation of impingement erosion using single particles , 1972 .

[18]  S. A. Morsi,et al.  An investigation of particle trajectories in two-phase flow systems , 1972, Journal of Fluid Mechanics.

[19]  G. Tilly Erosion caused by airborne particles , 1969 .

[20]  B. Launder,et al.  The numerical computation of turbulent flows , 1990 .

[21]  I. Finnie Erosion of surfaces by solid particles , 1960 .

[22]  Widen Tabakoff,et al.  Review—Turbomachinery Performance Deterioration Exposed to Solid Particulates Environment , 1984 .