首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >LDV measurements and analysis of gas and particulate phase velocity profiles in a vertical jet plume in a 2D bubbling fluidized bed Part III: The effect of fluidization
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LDV measurements and analysis of gas and particulate phase velocity profiles in a vertical jet plume in a 2D bubbling fluidized bed Part III: The effect of fluidization

机译:LDV测量和二维鼓泡流化床中垂直射流羽流中气相和颗粒相速度分布的分析和分析第三部分:流化的影响

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摘要

In the present work, the effect of emulsion fluidization on the gas and particle phase transport in a highspeed gas jet plume in a bubbling bed is examined. Implementing a Laser Doppler Velocimetry (LDV) technique, the gas and particulate phase velocities of a gas jet injected into a bubbling bed of 838 μm high-density polyethylene (HDPE) micropellets were measured. These velocity profiles were used to determine the volume fraction, mass flow, and momentum transport rate for each phase at various axial locations as well as an average particle drag coefficient in the measurement region of the plume. Maintaining consistent gas jet inlet conditions, the HDPE emulsion fluidization was varied from a spouted bed to 50% beyond minimum fluidization. In addition to the integral flow values, centerline phase velocity scaling is also examined. The scaling is based on the development of similarity velocity profiles for the two phases. Additional experiments to investigate this idea were carried out with 1) the particle emulsion and fluidization level is held constant while the jet inlet velocity is varied and 2) the jet inlet velocity and fluidization ratio is held constant while the bed particles are varied.
机译:在目前的工作中,研究了乳化剂流化对鼓泡床中高速气体喷射羽流中气相和颗粒相传输的影响。通过实施激光多普勒测速(LDV)技术,测量了注入838μm高密度聚乙烯(HDPE)微丸的沸腾床中的气体射流的气相和颗粒相速度。这些速度曲线用于确定在不同轴向位置上每个相的体积分数,质量流量和动量传输率,以及羽流测量区域中的平均颗粒阻力系数。为了保持一致的气体入口条件,HDPE乳液的流态化从喷床到超出最小流态化的50%。除了积分流量值外,还检查了中心线相速度定标。缩放基于两个阶段的相似速度曲线的发展。为了进一步研究这个想法,还进行了以下实验:1)在改变射流入口速度的同时保持颗粒乳液和流化水平恒定,以及2)在改变床层粒子的同时使射流入口速度和流化比率保持恒定。

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