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Discrete Particle Simulation of Heat Transfer in Pressurized Fluidized Bed with Immersed Cylinders

机译:加压流化床中传热离散粒子模拟浸入式圆柱体

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The combined computational fluid dynamics and discrete element method (CFD-DEM) has been extended and used in recent years to study heat transfer between bed and an immersed cylinder in fluidized beds at the particle scale. The previous models usually assume the gas flow to be two-dimensional. This does not fully represent the reality in which both the gas motions and particle-gas interactions naturally have more than six degrees of freedom. Here, a full 3DCFD-DEM model is developed to study the heat transfer in 3D gas-fluidized beds with immersed cylinders. For the purpose of the model validation, the simulations are conducted first for a single cylinder under different superficial gas velocities. It is shown that the predicted heat transfer coefficients between the cylinder and bed as a function of superficial gas velocity qualitatively agree with the measurements reported in the literature. The v-shaped curve is also reproduced. Then the simulations are conducted for a fluidized bed with cylinder banks (inline and staggered configurations) at a moderate superficial gas velocity. It is also shown that there is no significant difference in the averaged heat transfer coefficient between inline and staggered arrangements at a moderate superficial gas velocity. This work demonstrates that the developed 3D CFD-DEM approach could be a useful tool to study the coupled flow phenomena and heat transfer in such complex systems.
机译:近年来,组合的计算流体动力学和分立元件方法(CFD-DEM)已经延伸和使用,以在颗粒规模的流化床中研究床和浸入式圆筒之间的热传递。以前的模型通常假设气流是二维的。这并未完全代表天然气运动和颗粒 - 气体相互作用自然具有超过六个自由度的现实。这里,开发了完整的3DCFD-DEM模型,以研究3D气体流化床中的传热,浸入圆柱体。出于模型验证的目的,模拟首先在不同浅表气体速度下进行单个汽缸进行。结果表明,汽缸和床之间的预测传热系数作为浅表气体速度的函数定性地同意文献中报道的测量。还再现V形曲线。然后,在适度的浅表气体速度下,用气缸组(内联和交错配置)进行模拟。还表明,在适度的浅表气体速度下在线和交错布置之间的平均传热系数没有显着差异。这项工作表明,开发的3D CFD-DEM方法可以是研究这种复杂系统中的耦合流动现象和传热的有用工具。

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