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首页> 外文期刊>Experimental Thermal and Fluid Science: International Journal of Experimental Heat Transfer, Thermodynamics, and Fluid Mechanics >Experimental studies on a corrugated plate heat exchanger for small temperature difference applications
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Experimental studies on a corrugated plate heat exchanger for small temperature difference applications

机译:小温差应用的波纹板式换热器的实验研究

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摘要

Experimental studies were performed on a corrugated plate heat exchanger for small temperature difference applications. Experiments were performed on a single corrugation pattern on 20 plates arranged parallelly, with a total heat transfer area of 1.16298m~2. The spacing, ΔX, between the plates was varied (ΔX=6mm, 9mm, and 12mm) to experimentally determine the configuration that gives the optimum heat transfer. Water was used on both the hot and the cold channels with the flow being parallel and entering the heat exchanger from the bottom. The hot water flowrates were varied. The cold side flowrate and the hot and cold water inlet temperatures were kept constant. It is found that for a given ΔX, the average heat transfer between the two liquids increases with increasing hot water flowrates. The corrugations on the plates enhance turbulence at higher velocities, which improves the heat transfer. The optimum heat transfer between the two streams is obtained for the minimum spacing of ΔX=6mm. The pressure losses are found to increase with increasing flowrates. The overall heat transfer coefficients, U, the temperature difference between the two stream at outlet, and the thermal length are also presented for varying hot water flowrates and ΔX. The findings from this work would enhance the current knowledge in plate heat exchangers for small temperature difference applications and also help in the validation of CFD codes.
机译:在小温差应用的波纹板式换热器上进行了实验研究。在20个平行排列的板上进行单一波纹图案的实验,总传热面积为1.16298m〜2。改变板之间的间距ΔX(ΔX= 6mm,9mm和12mm),以实验确定提供最佳传热的构造。在热通道和冷通道上都使用水,水流平行并且从底部进入热交换器。热水流量是变化的。冷侧流量和冷热水入口温度保持恒定。发现对于给定的ΔX,两种液体之间的平均热传递随着热水流量的增加而增加。板上的波纹在较高的速度下增加了湍流,从而改善了热传递。在最小间距ΔX= 6mm的情况下,获得了两个流之间的最佳传热。发现压力损失随着流量的增加而增加。对于不同的热水流量和ΔX,还给出了总的传热系数U,出口两股水流之间的温差以及热长度。这项工作的发现将增强小温差应用中板式换热器的现有知识,并有助于CFD代码的验证。

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