Detached eddy simulation of particle dispersion in a gas-solid two-phase fuel rich/lean burner flow

Fuel ◽  
2005 ◽  
Vol 84 (6) ◽  
pp. 723-731 ◽  
Author(s):  
H ZHOU ◽  
K CEN ◽  
J FAN
Author(s):  
Russell Prater ◽  
Yongsheng Lian

The internal flows of high pressure diesel injectors are simulated numerically in order to investigate the complex transient flow structures and the unsteady forces imparted to the injector needle that result. The gas-liquid two phase flow is modeled using a mixture schematic with the cavitation numerically modeled using the Zwart-Gerber-Belamri model. Both the k-ε model and the detached eddy simulation (DES) model are used and the numerical results are compared. Our study shows that the DES model is able to capture the important unsteady flow features missed by the k-ε model. Our simulation also shows that the injector geometry, specifically the gain orifice, plays an important role in the forces developed on the injector needle.


Author(s):  
M. Fairweather ◽  
J. Yao

A particle-laden turbulent flow in a square duct is predicted using large eddy simulation (LES). The simulation is performed for a Reynolds number of 35,500, and correctly predicts the existence of secondary flows and their effects on the mean flow. The results are also in good qualitative agreement with experimental data obtained at different Reynolds numbers. One-way coupling is assumed between solid particles and the fluid, and a particle equation of motion, including Stokes drag, lift, buoyancy and gravity force terms, solved using a Lagrangian particle tracking technique. Three sizes of particle (1, 50 and 100 μm) are considered, and results demonstrate that size has a significant effect on particle dispersion and deposition in the duct flow. As particle size increases, therefore, they tend to settle on the floor of the duct, with less dispersion in the fluid phase. The study demonstrates the usefulness of LES for nuclear waste processing applications since secondary flows occur in many practically-relevant flows, and since it is desirable that the two-phase waste mixture is kept as homogeneous as possible to prevent, or at least discourage, the settling out of solid particles to form a bed which can promote pipe blockages.


Author(s):  
Bing Wang ◽  
Hui-Qiang Zhang ◽  
Xi-Lin Wang ◽  
Yin-Cheng Guo ◽  
Wen-Yi Lin

Numerical simulations of the two-dimensional backward facing step gas-particle turbulent flow are reported. Both the evolution of large eddy coherent structures in spatially and temporally and the vortex-particle interactions are researched. Effects of the particle Stokes number and the initial two-phase velocity slip on the instantaneous concentration distribution of the particles with and without the influence of gravity are discussed. Continuous phase simulation is performed by the method of large eddy simulation (LES) while the particle phase is solved by a Lagrangian method. Simulations of the gas phase reproduce the character of the separation and reattachment flow and the essential features of the coherent structures. It is shown that the vortex structures become extraordinary abundant and complex under the high Reynolds number. Further more, the simulation shows the initial two-phase velocity slip plays an important role in enforcing particle dispersion and sharply changes the instantaneous particle distribution under the different particle Stokes numbers. Even more, results demonstrate the influence of gravity on particle dispersion and sedimentation. Such pronounces effect of gravity on instantaneous concentration of particles with increased Stokes number and initial slip coefficients emphasize the need for the consideration of gravity for horizontal particle-laden flow. Either the continuous phase results or particle phase results obtained from LES agree well with the experiment data both in quantitative and qualitative.


Author(s):  
Mo Yang ◽  
Dan Su ◽  
Yuwen Zhang ◽  
Zhangyang Kang

Numerical simulation of anti-rich/lean burner jet flow is carried out to simulate two forms of gas-solid two-phase jet fields. One is a single burners and its exit of certain areas gas-solid two-phase jet field. Another one is gas-solid two-phase jet field in the single-layer combustion region. Predication of the particle dispersion in the burner jet is of great importance in industrial application and in the designing of coal burner with good performance. The objective of this study is to numerically investigate the particle dispersion mechanisms in the gas–solid two-phase jet from an anti-rich/lean burner. The detached-eddy-simulation (DES) approach is employed to study the turbulent flow in the fuel rich/lean separator and the gas–solid multiphase jet from the exit of an anti-rich/lean burner. The numerical results show that adding bias current of anti-rich/lean burner exit jet flow keeps anti-rich/lean of properties. Since the exit of boundary air speed is almost twice of primary air velocity, boundary air act on coal powder flow in acceleration and conveying, coal powder flow can keep boiler of inscribed circle position.


2010 ◽  
Vol 21 (07) ◽  
pp. 867-890 ◽  
Author(s):  
BING WANG ◽  
HUIQIANG ZHANG ◽  
XILIN WANG

This paper evaluates three widely used particle stochastic separated flow (SSF) models through large eddy simulation (LES) of gas-particle two-phase turbulent flows over a backward-facing step. The ability of the models to predict mean velocities, fluctuating velocities, and spatial dispersion of particles are carefully examined in comparison with LES reference results. Evaluation shows that the improved time-series SSF model produces good predictions on mean and fluctuating velocities in the particle phase which highly agree with LES results. However, the time-series SSF model has higher computational cost. Further, compared with the two other models, the time-series SSF model predicts better results on the spatial dispersion of particles. It has an overall advantage in terms of accuracy and efficiency in predicting velocity moments and particle dispersion even without the presence of so many particles. The dependence of different SSF models on the number of computational particles in a converged flow field is also discussed. This paper is useful for the selection and application of SSF models in numerical simulations of practical two-phase turbulent flows.


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