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Numerical Simulation and Mechanism of Heat Transfer in Quenching Fluidised Beds

机译:淬火流化床传热的数值模拟与机理

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In this work, a computational model is developed to simulate heat transfer between fluidised bed and workpiece surface, based on the particle group configuration deduced by the method of minimum energy loss of gas flowing through the bed. The heat transfer flux from the surface of workpieces to fluidised beds is controlled by dense gas-solid emulsion and bubble phases, alternately. Based on the simulation results, the heat transfer mechanism is analysed. The results show that the heat transfer coefficient on the immersed surface near particle is about 6-10 times of that on other areas. The section with a high heat transfer coefficient is in the circle area with a diameter of 0.75d_p. The heat transfer between the fluidised beds and the workpiece surface is mainly contributed by the conduction in still gas film of 0.12d_p thick.
机译:在这项工作中,基于通过流经床层的气体的最小能量损失方法推导的粒子群构型,开发了一个计算模型来模拟流化床和工件表面之间的传热。从工件表面到流化床的传热通量是由致密的气固乳液和气泡相交替控制的。基于仿真结果,对传热机理进行了分析。结果表明,颗粒附近的浸没表面的传热系数约为其他区域的传热系数的6-10倍。传热系数高的部分位于直径为0.75d_p的圆形区域中。流化床与工件表面之间的热传递主要是由0.12d_p厚的静止气膜中的热传导引起的。

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