首页> 外文会议>ASME·JSME Thermal Engineering Joint Conference >CONVECTION HEAT TRANSFER OF AN OPEN RECTANGULAR CAVITY PACKED WITH SPHERICAL PARTICLES IN AN AIR FLOW (EFFECT OF CAVITY LENGTH)
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CONVECTION HEAT TRANSFER OF AN OPEN RECTANGULAR CAVITY PACKED WITH SPHERICAL PARTICLES IN AN AIR FLOW (EFFECT OF CAVITY LENGTH)

机译:在空气流中填充有球形颗粒的开放矩形腔的对流传热(腔长的效果)

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Forced-natural-mixed convection heat transfer characteristics of one-stage spherical particle layer are investigated experimentally. The one-stage spherical particle layer is provided in a rectangular cavity installed at the lower part of a rectangular channel. The test fluid (air) flows through the rectangular channel, and is heated by the bottom surface of the cavity via the particle layer. Three types of spherical particles, which have almost the same diameter of about 10 mm and different thermal conductivities are tested. The cavity length is varied in three steps of 20 mm, 43 mm and 90 mm, and the cavity depth is changed in four steps of 0 mm (flat plane), 2.5 mm, 5 mm, and 10 mm. The air velocity is ranged from 0.15 m/s to 2.5 m/s, and the temperature difference between the incoming air and the heating surface is varied between 10 K and 100 K. The particles placed on the heat transfer surface suppress the air flow near the heat transfer surface and reduce the heat transfer, while the particles also function as an extended heat transfer surface and a turbulence promoter. Since the particles have these two opposite effects, the heat transfer coefficient changes variously with changing of the experimental conditions. The heat transfer coefficient can be expressed as a non-dimensional heat transfer correlation, where the effects of the cavity length, the cavity depth, the air velocity and the temperature difference between the air and the bottom surface of the cavity are taken into consideration.
机译:实验研究了一级球形颗粒层的强制 - 自然混合对流传热特性。单级球形颗粒层设置在安装在矩形通道的下部的矩形腔中。测试流体(空气)流过矩形通道,并通过颗粒层被腔的底表面加热。测试了三种类型的球形颗粒,其具有约10mm和不同的导热率的直径。腔长在20mm,43mm和90mm的三个步骤中变化,并且腔深度以0mm(平面),2.5mm,5mm和10mm的四个步长。空气速度范围为0.15 m / s至2.5 m / s,并且进入空气和加热表面之间的温度差异在10k和100k之间变化。放置在传热表面上的颗粒抑制了附近的空气流量传热表面并减少传热,而颗粒也用作延长的传热表面和湍流启动子。由于颗粒具有这两个相反的效果,因此传热系数随着实验条件的改变而变化。传热系数可以表示为非尺寸传热相关性,其中,考虑了空腔长度,空腔深度,空气速度和空腔之间的温度差的效果。

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