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A CFD approach on the effect of particle size on char entrainment in bubbling fluidised bed reactors

机译:关于粒径对焦炭影响的CFD方法 在鼓泡流化床反应器中夹带

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摘要

The fluid – particle interaction inside a 41.7 mg s?1 fluidised bed reactor is modelled. Three char particles of sizes 500 ?m, 250 ?m, and 100 ?m are injected into the fluidised bed and the momentum transport from the fluidising gas and fluidised sand is modelled. Due to the fluidising conditions and reactor design the char particles will either be entrained from the reactor or remain inside the bubbling bed. The particle size is the factor that differentiates the particle motion inside the reactor and their efficient entrainment out of it. A 3-Dimensional simulation has been performed with a completele revised momentum transport model for bubble three-phase flow according to the literature as an extension to the commercial finite volume code FLUENT 6.2.
机译:对41.7 mg s?1流化床反应器内的流体-颗粒相互作用进行了建模。将三个大小分别为500?m,250?m和100?m的炭颗粒注入流化床中,并对流化气体和流化砂的动量传输进行建模。由于流化条件和反应器设计的原因,焦炭颗粒将从反应器中夹带或留在鼓泡床中。颗粒大小是区分颗粒在反应器内部运动和其有效夹带的因素。根据文献,对气泡三相流进行了完全修正的动量传递模型的三维模拟,作为商业有限体积代码FLUENT 6.2的扩展。

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