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Local heat transfer to surfaces immersed in the freeboard region of a fluidized bed.

机译:局部热传递到沉浸在流化床干舷区域中的表面。

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摘要

This work describes the local heat transfer in the freeboard region of a fluidized bed. Plate surface to particle suspension heat transfer coefficients in the freeboard of a fluidized bed (30 cm i.d.) have been measured by a newly designed miniature heating plate. Four types of plate orientations have been employed to investigate the directional effect of gas-solids flow to plate surface on the heat transfer rate. Local solids concentrations in the freeboard were also obtained by a nozzle-type sampling probe.; Results indicate that the heat transfer coefficient varies with axial and radial plate location, plate orientation, and gas velocities. Variations of heat transfer coefficients with radial position are more significant at lower freeboard heights than at higher ones for all the gas velocities (0.28-0.64 m/s) examined. For plates parallel to both the axial and radial directions of the column, the heat transfer coefficient (h) is higher at the center than at wall. The plate with exposed surface parallel to the axial and perpendicular to the radial directions gives nearly the same value of h at the center and the wall. At lower freeboard levels, the center-facing surface exhibits higher heat transfer rate than the wall-facing one, which can be explained from the higher solids concentration and center to wall movement of particles. Plate with downward exposed surface exhibits the highest heat transfer rate at high gas flow rates because of direct bombardment of solid particles splashed from the bed. Variations of heat transfer coefficients with elevation in the freeboard are as much as an order of magnitude. However, these variations with elevation are relatively insensitive to plate orientations investigated.; A surface-to-suspension heat transfer model has also been developed to elucidate the surface to particle heat transfer mechanism in this lean phase system. The proposed model can explain reasonably well the inter-dependence of the measured heat transfer coefficient, solids concentration, heat capacity, particle size, and solids velocity in the freeboard.
机译:这项工作描述了流化床干舷区域的局部传热。用新设计的微型加热板测量了流化床干舷(内径30厘米)中板表面到颗粒悬浮液的传热系数。已经采用四种类型的板取向来研究气固流向板表面的方向对传热速率的影响。干口中的局部固体浓度也通过喷嘴型采样探头获得。结果表明,传热系数随轴向和径向塔板位置,塔板方向以及气体速度而变化。对于所研究的所有气体速度(0.28-0.64 m / s),较低的干舷高度处的传热系数随径向位置的变化要比较高的干舷处的变化大。对于平行于柱的轴向和径向的板,中心的传热系数(h)高于壁的传热系数(h)。具有平行于轴向且垂直于径向的暴露表面的板在中心和壁处给出几乎相同的h值。在较低的干舷水平下,面向中心的表面比面向壁的表面表现出更高的传热速率,这可以从较高的固体浓度和颗粒中心向壁的运动来解释。具有向下暴露表面的板在高气流速率下表现出最高的传热率,因为直接轰击了从床中溅出的固体颗粒。干舷中传热系数随高度的变化高达一个数量级。然而,这些随高度的变化对所研究的板的方向相对不敏感。还开发了表面到悬浮体的传热模型,以阐明此稀相系统中表面到颗粒的传热机理。提出的模型可以很好地解释干舷中测得的传热系数,固体浓度,热容量,粒径和固体速度之间的相互依赖性。

著录项

  • 作者

    Tsai, Kun-Yung.;

  • 作者单位

    University of New Hampshire.;

  • 授予单位 University of New Hampshire.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 1991
  • 页码 321 p.
  • 总页数 321
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 化工过程(物理过程及物理化学过程);
  • 关键词

  • 入库时间 2022-08-17 11:50:27

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