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An experimental investigation of wall-bed heat transfer and flow characteristics in a swirling fluidized bed reactor

机译:旋流流化床反应器中壁床传热和流动特性的实验研究

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The present work investigates the heat transfer between the immersed heater and bed and hydrodynamics of the bed in swirling fluidized bed. The heat transfer process and bed hydrodynamics characteristics for swirling fluidized bed reactor (SFBR) were compared to those of conventional fluidized bed reactor (CFBR). Then the influence of particle diameter on the bed flow characteristics and heat transfer process in SFBR were studied. The heat transfer coefficient was calculated at different superficial air velocities, radial positions, and bed heights. Compared to a CFBR, the bed pressure drop and distributor pressure drop for SFBR were lower, that characterizes swirling bed reactor. The heat transfer coefficient of SFBR was higher than the corresponding of CFBR at lower portion of the bed and it was lower at the upper portion of the bed for all radial positions and for all air superficial velocities. Increasing particle diameter in SFBR resulted in decreasing both the heat transfer coefficient and bed pressure drop.
机译:目前的作品研究了旋转流化床中浸渍加热器和床和床的流体动力学之间的传热。将用于旋流流化床反应器(SFBR)的传热过程和床流体动力学特性与常规流化床反应器(CFBR)进行比较。然后,研究了粒径对SFBR床流动特性和传热过程的影响。在不同的浅表空气速度,径向位置和床高度下计算传热系数。与CFBR相比,SFBR的床压降和分配器压降较低,表征旋转床反应器。 SFBR的传热系数高于床下的下部的CFBR的对应,并且在床的上部处于所有径向位置和所有空气浅表速度下降。在SFBR中增加粒径导致传热系数和床压降的降低。

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