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PARTICLE TO GAS HEAT TRANSFER IN A CIRCULATING FLUIDIZED BED (CFB) RISER

机译:循环流化床(CFB)立管中的气体传热颗粒

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The main objective of this study was to measure the heat transfer from particle to gas in a dilute CFB riser (ε > 0.8) and to derive a predictive equation for the local particle-gas heat transfer coefficient. This coefficient was found to be a strong function of the particle velocity, concentration and length of the heat transfer section. Accordingly, a new correlation in terms of these parameters is proposed.
机译:这项研究的主要目的是测量稀释的CFB立管中从颗粒到气体的热传递(ε> 0.8),并得出局部颗粒-气体热传递系数的预测方程。发现该系数与传热段的颗粒速度,浓度和长度密切相关。因此,提出了关于这些参数的新的相关性。

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