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DIRECT CONTACT HEAT EXCHANGE BETWEEN PARTICLES AND A HEAT TRANSFER SURFACE IN A FLUIDIZED BED

机译:在流化床中直接接触颗粒和传热表面之间的热交换

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Direct-contact heat exchange between fluidizing solid particles and a heat transfer surface, which is one of the most effective heat transfer mechanisms in a fluidized bed, has been investigated. The temperature of the fluidizing particles during the period of contact with a heat transfer surface is visualized by using an Infrared (IR) imager. Based on the visualized temperature of the particles, the contact conductance between a single particle and the heat transfer surface was determined by inverse analyses. A schematic diagram of the experimental setup is shown in Fig. A-1. Visualization of particle temperature and observation of the contact status between the particles and the heat transfer surface were performed through the heat transfer surface, which is made of a MgF{sub}2 window, so as not to disturb the particle fluidization. An IR imager located external to the bed was used to visualize the temperature of the fluidizing particles heated by the heat transfer surface and a conventional VTR camera to observe the contact status. A CO{sub}2 laser was used to remotely heat the heat transfer surface so as not to obstruct visualization of the IR imager and the VTR camera. This visualization system allows measurement of the particle temperature during the contact period. Two different inverse analyses are adopted for determining the contact conductance. In one of them, the particle temperature is assumed to be uniform, and in the other, the temperature distribution within the particles is rigorously considered. The estimated contact conductance is tabulated for several particle diameters and fluidizing velocities, and their effects on the contact conductance are discussed. The contact Nusselt numbers as well as the contact conductance are determined, and are compared with Decker's prediction. The present contact Nusselt numbers, which are determined by the inverse analysis where the temperature distribution in the particles are rigorously considered, are close to Decker's prediction.
机译:已经研究了流化固体颗粒和传热表面之间的直接接触热交换,该热传递表面是流化床中最有效的传热机制之一。通过使用红外(IR)成像器,可视化在与传热表面接触期间的流化颗粒的温度。基于颗粒的可视化温度,通过逆分析确定单个颗粒和传热表面之间的接触电导。实验设置的示意图如图2所示。a-1。通过传热表面进行粒子温度和观察颗粒和传热表面之间的接触状态的观察,该传热表面由MgF {u} 2窗制成,以免干扰颗粒流化。位于床外部的IR成像器用于可视化由传热表面加热的流化颗粒的温度和传统的VTR摄像机以观察接触状态。 CO {Sub} 2激光器用于远程加热传热表面,以免妨碍IR成像器和VTR相机的可视化。该可视化系统允许在接触期间测量粒子温度。采用两种不同的逆分析来确定接触电导。在其中一个中,假设颗粒温度是均匀的,并且在另一方面,颗粒内的温度分布严格考虑。估计的接触电导是针对几个粒径和流化速度制成的,并且讨论了它们对接触电导的影响。确定接触露珠数以及接触电导,并与甲板的预测进行比较。本发明的触点露珠数由逆分辨率分布严格考虑的逆分析确定,接近甲板的预测。

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