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Extension of the model of binary fluidization to beds confined in a packing of coarse spheres

机译:将二元流化模型扩展到限制在粗球体填料中的床

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摘要

The prediction of the minimum fluidization velocity of beds of Geldart's group B particles confined in a packed bed of coarse spheres can be achieved by extending to this peculiar type of systems the theory developed for modelling the behaviour of segregating beds of simultaneously fluidized solids. The approach is based on separate force balances on the fluid and the fine solids, capable to account for the peculiar nature of solid-solid interaction in a confined fluidized bed. Its validation is fulfilled by an extended investigation conducted in two columns (5 and 10 cm OD) packed with a fixed bed of 4.1 mm lead shots or 11 mm glass beads. The effect of particle size on the fluidization regime is investigated by comparing the results provided by experiments in which various cuts of glass ballotini, ranging from 100 to nearly 600 μm, are fluidized in two packings of fixed spheres; possible differences of behaviour due to particle density are analysed by series of experiments employing particles of ceramics, zirconium oxide, steel and bronze of the same diameter. The results obtained confirm the effectiveness of the approach followed, in which an important role is played by the indirect interaction between the two solid phases.
机译:可以通过将用于模拟同时流化固体的分离床行为的理论扩展到这种特殊类型的系统,来预测局限在粗球填充床中的Geldart B组颗粒床的最小流化速度。该方法基于在流体和细固体上的单独的力平衡,能够解释密闭流化床中固-固相互作用的特殊性质。通过对两根色谱柱(外径分别为5和10 cm)进行了广泛的研究,该色谱柱装有4.1 mm铅丸或11 mm玻璃珠的固定床。通过比较实验结果,研究了粒径对流态化的影响,在实验中,将100至近600μm范围的各种玻璃巴洛蒂尼切块流化成两个固定球状填料;通过使用相同直径的陶瓷,氧化锆,钢和青铜的颗粒的一系列实验,分析了由于颗粒密度引起的可能的行为差异。获得的结果证实了所采用方法的有效性,其中两个固相之间的间接相互作用起着重要作用。

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