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CFD modeling of mixing/segregation behavior of biomass and biochar particles in a bubbling fluidized bed

机译:鼓泡流化床中生物质和生物炭颗粒混合/分离行为的CFD建模

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Computational Fluid Dynamics (CFD) simulations have been carried out to examine the hydrodynamics of a mixture of biomass and biochar particles in a bubbling fluidized bed. The effect of superficial gas velocity, biomass density and particle size on the mixing/segregation behavior of biomass-biochar mixture was analyzed using the Euler-Euler (EE) model. It was observed that on increasing the superficial gas velocity, the bubbles size increased which led to better mixing of both biomass and biochar particles. The biomass density had a significant impact, but particle size had a little impact on the distribution of biomass particles in the biochar bed. Simulations were conducted in both 2-dimensionaI (2-D) and 3-dimensionaI (3-D) configurations, and were validated using the available experimental data. A sensitivity analysis was also carried out for examining the effect of different gas-solid drag correlations, wall boundary conditions and particle-particle restitution coefficient. For the operating conditions considered in this study, it was determined that the choice of drag coefficient correlation, particle-wall and particle-particle interaction parameters had a considerable impact on the hydrodynamics of the biomass-biochar mixture.
机译:已经进行了计算流体动力学(CFD)模拟,以检查鼓泡流化床中生物质和生物炭颗粒混合物的流体动力学。利用Euler-Euler(EE)模型分析了表观气体速度,生物质密度和粒径对生物质-生物炭混合物混合/分离行为的影响。观察到,随着表观气体速度的增加,气泡的尺寸增加,这导致生物质和生物炭颗粒的更好混合。生物质密度具有显着影响,但粒径对生物炭床中生物质颗粒的分布影响很小。在2-dimensionaI(2-D)和3-dimensionaI(3-D)配置中均进行了仿真,并使用可用的实验数据进行了验证。还进行了敏感性分析,以检查不同气固阻力相关性,壁边界条件和颗粒-颗粒复原系数的影响。对于本研究中考虑的运行条件,确定了阻力系数相关性,颗粒-壁和颗粒-颗粒相互作用参数的选择对生物质-生物炭混合物的流体动力学有很大影响。

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