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Heat transfer and flow friction characteristics of perforated plate heat exchangers.

机译:多孔板式换热器的传热和流动摩擦特性。

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An experimental study of perforated plate heat transfer surfaces for application in recuperative beat exchangers for a solid hydrogen sorption cryocooler stage has been performed in order to identify suitable perforated surfaces, and to evaluate their performance. Friction factors and heat transfer coefficients have been obtained experimentally for a range of perforated surfaces with flow normal to the surface for Reynolds number less than 25. The single-blow transient testing method was used to obtain the heat transfer coefficients and the friction factors were obtained from isothermal pressure drop tests. The heat transfer data was processed using the "maximum-slope" technique. The data reduction model includes axial fluid and spacer conduction, compressibility and slip-flow effects, a step-wise temperature profile and assumes an exponential inlet temperature response. The results demonstrate a good thermal hydraulic performance for the surfaces tested at low Reynolds number. A model of a perforated plate counterflow exchanger which includes axial conduction and a step-wise temperature profile was used to evaluated the surfaces tested. A suitable perforated plate exchanger design has been identified which meets the design goal for a solid hydrogen sorption cryocooler stage of 95% efficiency.
机译:为了确定合适的穿孔表面并评估其性能,已经进行了用于板式换热器中的多孔板传热表面的实验研究,该换热器用于固体氢吸收式低温冷却器。通过实验获得了一系列流动表面的摩擦因数和热传递系数,这些流动表面的流动与雷诺数小于25的法线垂直。使用单吹瞬变测试方法获得热传递系数,并获得了摩擦系数来自等温压降测试。传热数据使用“最大斜率”技术处理。数据减少模型包括轴向流体和隔离物的传导,可压缩性和滑流效应,逐步温度曲线,并假定指数入口温度响应。结果证明了在低雷诺数下测试的表面具有良好的热水力性能。使用包括轴向传导和逐步温度分布的多孔板逆流交换器模型来评估测试的表面。已经确定了一种适合的多孔板式换热器设计,该设计可以满足效率为95%的固态氢吸收式低温冷却器级的设计目标。

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