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Friction between gas-solid flow and circulating fluidized bed downer wall

机译:气固两相流与循环流化床下部壁之间的摩擦

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摘要

Friction between co-current downflow gas-solid flow and column wall was investigated by measuring apparent and actual solids concentrations in a circulating fluidized bed (CFB) downer. A new model to predict pressure drops due to friction between the gas-solid suspension in the fully developed zone and the downer wall was developed. The results show that the friction between the gas-solid suspension and the downer wall causes a significant deviation of the apparent solids concentrations from the actual ones, especially for those operating conditions with higher superficial gas velocities and solids circulation rates. When the superficial gas velocity is greater than 8 m/s, the actual solids concentrations in the fully developed region of the downer can be up to two to three times of the apparent values. Particle diameters have different influences on the frictional pressure drops under different superficial gas velocity. After the frictional pressure drop is considered, the predicted actual solids concentrations by the proposed model agree well with the experimental values.
机译:通过测量循环流化床(CFB)下降器中的表观和实际固体浓度,研究了并流下降气流的气固两相流和柱壁之间的摩擦。开发了一种新的模型,该模型可预测由于充分展开区域中的气固悬浮液和下壁之间的摩擦而引起的压降。结果表明,气固悬浮液和下壁之间的摩擦力导致表观固体浓度与实际浓度明显偏离,特别是对于那些具有较高表观气体速度和固体循环速率的运行条件。当表观气体速度大于8 m / s时,下降管充分展开区域中的实际固体浓度可能高达表观值的2至3倍。在不同的表观气体速度下,粒径对摩擦压降有不同的影响。考虑了摩擦压降后,所提出的模型预测的实际固体浓度与实验值吻合良好。

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