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SOLIDS CIRCULATION IN THE JETTING REGION OF A FLUIDIZED BED.

机译:流化床接缝区域中的固体循环。

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The purpose of this study was to analyze particle circulation, and reactions in the jet region of a fluidized bed. The two fundamental questions addressed here related to the measurement of particle velocities in the grid region of a fluidized bed, and to the relevance of the jet zone to the operation of a fluidized bed reactor.; An optical fiber probe anemometer, capable of measuring the velocities of solids moving in two-phase flows, was constructed. Three optical fiber probes were designed: one suitable for use in measuring the local average velocities of solid particles moving in flat beds; another, to measure instantaneous velocity; and a third, having high directional sensitivity.; Particle velocities were measured at corresponding points with a jet in a two-dimensional bed, using the optical fiber probe, and also using a Laser Doppler Velocimeter (LDV). The probe measurements compare well with the LDV results. Particle velocities were also measured using the probe, in the dense phase region of the bed, where measurements were not possible using the LDV. The resulting flow maps clearly indicate solids circulation patterns around jets, and identify dead zones formed on the distributor plate. The measurements also show that the assumption of two-dimensional behavior in flat beds is valid, except in the immediate neighborhood of grid orifices, since no significant velocity differences were observed across the thickness of the bed.; A mathematical model for solids motion in the inlet jet was developed from first principles, based on the particle momentum balance and continuity equations. The simulation results compare well with the experimentally measured particle velocities, when gas percolation from the spout to the annulus is taken into account.; A gas jet entering a fluidized bed coal combustor, was modeled. Typical conditions for a fluidized bed combustor were used, and the model includes the reactions between carbon and carbon dioxide and oxygen, and the homogeneous oxidation of carbon monoxide. The results indicate that considerable reaction occurs in the gas jets entering a combustor, and that they should be considered in any careful analysis of its operation.
机译:本研究的目的是分析流化床射流区域的颗粒循环和反应。这里涉及的两个基本问题与流化床网格区域中颗粒速度的测量以及射流区与流化床反应器操作的相关性有关。构造了一种光纤探针风速仪,它能够测量在两相流中移动的固体的速度。设计了三种光纤探头:一种适合用于测量在平板中移动的固体颗粒的局部平均速度;另一种适合于测量在平板中移动的固体颗粒的局部平均速度。另一个,用于测量瞬时速度;第三,具有高的方向灵敏度。使用光纤探针,还使用激光多普勒测速仪(LDV),在二维床中通过射流在相应的点测量粒子速度。探头测量结果与LDV结果很好地比较。还使用探针在床的密相区域中测量了粒子速度,在该区域无法使用LDV进行测量。生成的流图清楚地表明了射流周围的固体循环方式,并确定了分布板上形成的死区。测量结果还表明,在平板床中二维行为的假设是有效的,除了在网格孔的紧邻区域内,因为在整个床厚上都没有观察到明显的速度差异。基于粒子动量平衡和连续性方程,从第一原理出发,建立了入口射流中固体运动的数学模型。当考虑到从喷口到环空的气体渗透时,模拟结果与实验测得的粒子速度很好地比较。对进入流化床煤燃烧器的气体射流进行了建模。使用流化床燃烧器的典型条件,该模型包括碳与二氧化碳和氧气之间的反应以及一氧化碳的均匀氧化。结果表明,进入燃烧室的气体射流会发生相当大的反应,在对其运行进行任何仔细分析时都应考虑到它们。

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