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Computational fluid dynamics modelling of biomass fast pyrolysis in fluidised bed reactors, focusing different kinetic schemes

机译:流化床反应器中生物质快速热解的计算流体动力学模型,关注不同的动力学方案

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The present work concerns with CFD modelling of biomass fast pyrolysis in a fluidised bed reactor. Initially, a study was conducted to understand the hydrodynamics of the fluidised bed reactor by investigating the particle density and size, and gas velocity effect. With the basic understanding of hydrodynamics, the study was further extended to investigate the different kinetic schemes for biomass fast pyrolysis process. The Eulerian-Eulerian approach was used to model the complex multiphase flows in the reactor. The yield of the products from the simulation was compared with the experimental data. A good comparison was obtained between the literature results and CFD simulation. It is also found that CFD prediction with the advanced kinetic scheme is better when compared to other schemes. With the confidence obtained from the CFD models, a parametric study was carried out to study the effect of biomass particle type and size and temperature on the yield of the products. (C) 2016 The Authors. Published by Elsevier Ltd.
机译:本工作涉及流化床反应器中生物质快速热解的CFD模拟。最初,进行了一项研究,通过研究颗粒的密度和大小以及气体速度的影响来理解流化床反应器的流体动力学。在对流体动力学有基本了解的情况下,该研究进一步扩展为研究生物质快速热解过程的不同动力学方案。欧拉-欧拉方法用于模拟反应器中的复杂多相流。将模拟所得产品的产率与实验数据进行比较。文献结果与CFD仿真之间取得了很好的比较。还发现,与其他方案相比,采用高级动力学方案的CFD预测更好。利用从CFD模型获得的置信度,进行了参数研究,以研究生物质颗粒类型,大小和温度对产品收率的影响。 (C)2016作者。由Elsevier Ltd.发布

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