Experimental studies on particle behaviour and turbulence modification in horizontal channel flow with different wall roughness

Abstract. Detailed measurements in a developed particle-laden horizontal channel flow (length 6 m, height 35 mm, the length is about 170 channel heights) are presented using phase-Doppler anemometry for simultaneous determination of air and particle velocity. The particles were spherical glass beads with mean diameters in the range of 60 µm–1 mm. The conveying velocity could be varied between about 10 m/s and 25 m/s, and the particle mass loading could reach values of about 2 (the mass loading is defined as the ratio of particle to gas phase mass flow rates), depending on particle size. For the first time, the degree of wall roughness could be modified by exchanging the wall plates. The influence of these parameters and the effect of inter-particle collisions on the profiles of particle mean and fluctuating velocities and the normalised concentration in the developed flow were examined. It was shown that wall roughness decreases the particle mean velocity and enhances fluctuating velocities due to irregular wall bouncing and an increase in wall collision frequency, i.e. reduction in mean free path. Thereby, the larger particles are mainly more uniformly distributed across the channel, and gravitational settling is reduced. Both components of the particle velocity fluctuation were reduced with increasing mass loading due to inter-particle collisions and the momentum loss involved. Moreover, the effect of the particles on the air flow and the turbulent fluctuations was studied on the basis of profiles in the developed flow and turbulence spectra determined for the streamwise velocity component. In addition to the effect of particle size and mass loading on turbulence modulation, the influence of wall roughness was analysed. It was clearly shown that increasing wall roughness also results in a stronger turbulence dissipation due to two-way coupling.

[1]  P. Moin,et al.  Numerical investigation of turbulent channel flow , 1981, Journal of Fluid Mechanics.

[2]  William C. Reynolds,et al.  Measurements in fully developed turbulent channel flow , 1975 .

[3]  John R. Fessler,et al.  Particle response and turbulence modification in fully developed channel flow , 1994, Journal of Fluid Mechanics.

[4]  Martin Sommerfeld,et al.  Characterization of the cross-sectional particle concentration distribution in pneumatic conveying systems , 1994 .

[5]  Dragoslav Milojevié Lagrangian Stochastic‐Deterministic (LSD) Predictions of Particle Dispersion in Turbulence , 1990 .

[6]  N. Huber,et al.  Experimental analysis and modelling of particle-wall collisions , 1999 .

[7]  S. Ziada,et al.  PDA measurements of droplet size and mass flux in the three-dimensional atomisation region of water jet in air cross-flow , 2000 .

[8]  Martin Sommerfeld,et al.  MODELLING OF PARTICLE-WALL COLLISIONS IN CONFINED GAS-PARTICLE FLOWS , 1992 .

[9]  Martin Sommerfeld,et al.  Modelling and numerical calculation of dilute-phase pneumatic conveying in pipe systems , 1998 .

[10]  Franz Durst,et al.  High-resolution data processing for phase-Doppler measurements in a complex two-phase flow , 1991 .

[11]  Shozaburo Saito,et al.  ON THE MECHANISM OF SUSPENSION OF PARTICLES IN HORIZONTAL PNEUMATIC CONVEYING: MONTE CARLO SIMULATION BASED ON THE IRREGULAR BOUNCING MODEL , 1970 .

[12]  C. Tropea,et al.  Single-Point Laser Measurement , 1999 .

[13]  Clayton T. Crowe,et al.  Effect of particle size on modulating turbulent intensity , 1989 .

[14]  Yohei K. Sato,et al.  Transport process of turbulence energy in particle-laden turbulent flow , 1996 .