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Mitigation of ice crystallization fouling in stationary and circulating liquid-solid fluidized bed heat exchangers

机译:固定和循环液固流化床换热器中冰晶结垢的缓解

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摘要

Liquid-solid fluidized bed heat exchangers are attractive ice crystallizers since they are able to mitigate ice crystallization fouling and exhibit high heat transfer coefficients. Experiments show that the fouling removal ability of stationary fluidized beds increases with decreasing bed voidage (95-80%) and increasing particle size (2-4 mm). The removal of ice crystallization fouling appears to be more effective in circulating fluidized beds, especially at high circulation rates. Fouling removal is realized by both particle-wall collisions and pressure fronts induced by particle-particle collisions. A comparison between ice crystallization experiments and impact characteristics shows that the removal rate is proportional to the impulse exerted on the wall. A model based on these phenomena is discussed and predicts the transition temperature difference for ice crystallization fouling in both stationary and circulating fluidized beds with an average absolute error of 9.2%.
机译:液固流化床热交换器是有吸引力的冰结晶器,因为它们能够减轻冰结晶结垢并显示出高的热传递系数。实验表明,固定流化床的除垢能力随床空隙率的降低(95-80%)和粒径(2-4 mm)的增加而增加。消除冰晶结垢似乎在循环流化床中更有效,尤其是在高循环速率下。通过颗粒壁碰撞和颗粒-颗粒碰撞引起的压力前沿来实现结垢去除。冰结晶实验和冲击特性之间的比较表明,去除率与施加在壁上的脉冲成正比。讨论了基于这些现象的模型,并预测了固定流化床和循环流化床中冰晶结垢的转变温度差,其平均绝对误差为9.2%。

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