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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Critical fluidization velocities and maximum bed pressure drops of homogeneous binary mixture of irregular particles in gas-solid tapered fluidized beds
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Critical fluidization velocities and maximum bed pressure drops of homogeneous binary mixture of irregular particles in gas-solid tapered fluidized beds

机译:气固锥形流化床中不规则颗粒的均相二元混合物的临界流化速度和最大床压降

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摘要

Recently,tapered fluidized bed has become more attractive because of the problems associated with conventional(cylindrical)beds like fluidization of widely distributed particles,entrainment of particles and limitation of fluidization velocity.There have been some investigations on hydrodynamics of uniform single size particles but there have been no detailed studies of homogeneous binary mixture of particles of different sizes and different particles in tapered beds.In the present work,an attempt has been made to study the hydrodynamic characteristics of homogeneous binary mixture of irregular particles in tapered beds having different tapered angles.Correlations have been developed for important characteristics,especially critical fluidization velocities and maximum bed pressure drops of homogeneous binary mixture of irregular particles in gas-solid tapered fluidized beds.Experimental values of critical fluidization velocities and maximum bed pressure drops have been compared with the developed correlations.
机译:近年来,锥形流化床由于与常规(圆柱形)床相关的问题而变得越来越有吸引力,例如广泛分布的颗粒的流化,颗粒的夹带和流化速度的限制。尚未对锥形床中不同粒径和不同颗粒的均相二元混合物进行详细的研究。本文试图研究不规则颗粒在锥角不同的锥形床中均质二元混合物的水动力特性。已经开发了重要特性的相关性,特别是临界流化速度和气固锥形流化床中不规则颗粒的均相二元混合物的最大床压降。已将临界流化速度和最大床压降的实验值进行了比较。发展的相关性。

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