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Large eddy simulation of biomass gasification in a bubbling fluidized bed based on the multiphase particle-in-cell method

机译:基于多相粒子细胞法的鼓泡流化床中生物质气化的大涡流模拟

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Numerical simulations of biomass gasification in a bubbling fluidized bed have been performed using a hybrid approach, where filtered gas-phase governing equations are solved in a Eulerian framework, and solid particles are modeled based on the multiphase-particle-in-cell method following Lagrangian stochastic parcel approach. A solver has been developed in OpenFOAM after incorporating both homogeneous and heterogeneous gasification reactions. Filtered governing equations of gas-phase variables are solved within the LES framework, where unresolved subgrid stresses and fluxes are obtained using the subgrid kinetic energy equation closure model. The solver could demonstrate transient flow characteristics of gas-solids flows in a fluidized bed, including formation, coalescence, and the eruption of bubbles at the bed surface. For different operating conditions such as steam/biomass ratio, equivalence ratio, and gasifier temperature, predicted concentrations of product gases at the gasifier outlet yield a good agreement with the experimental measurements. (C) 2020 Elsevier Ltd. All rights reserved.
机译:使用混合方法进行鼓泡流化床中生物质气化的数值模拟,其中滤波的气相控制方程在欧拉骨架中解决,基于拉格朗日后的多相粒子粒子细胞方法进行模拟固体颗粒随机包裹方法。在包含均匀和异质气化反应后,在OpenFoam中开发了一个求解器。在LES框架内求解气相变量的滤波控制方程,其中使用SubGrid动能方程闭合模型获得未解析的底图应力和助熔剂。求解器可以展示气体固体的瞬态流动特性在流化床中流动,包括形成,聚结和床面上的气泡喷发。对于诸如蒸汽/生物质比,等效比和气化器温度的不同的操作条件,气化器出口的产品气体的浓度与实验测量结果良好。 (c)2020 elestvier有限公司保留所有权利。

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