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首页> 外文期刊>Journal of Chemical Engineering of Japan >Heat Transfer Correlation in High Prandtl (High Schmidt) Number Fluid in Votator Type Scraped Surface Heat Exchanger
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Heat Transfer Correlation in High Prandtl (High Schmidt) Number Fluid in Votator Type Scraped Surface Heat Exchanger

机译:搅拌器式刮板式换热器中高普朗特(高施密特)数流体的传热相关性

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摘要

References(15) Cited-By(5) An experimental investigation to obtain heat transfer correlation in a Votator type scraped surface heat exchanger with two-blades was performed by an electro-chemical method. Measurements were carried by mass transfer under diffusion control in a ferricyanide/ferrocyanide redox electrochemical reaction. The heat transfer correlation was obtained from an analogy of heat and mass transfer. Local heat transfer coefficients on the wall of the outer column of the exchanger was measured by varying the rotational Reynolds number, flow rate of fluid, Prandtl number and equivalent diameter in order to obtain the unity thermal design equation.The time averaged local Nusselt number in a high Prandtl number fluid was found to be correlated by the following equation:Nu = 1.53Rer0.51Pr0.33 (Do/De)0.44 (1320 Pr Do/De Rer and De are the blade rotational Reynolds number and equivalent diameter respectively.
机译:参考文献(15)Cyted-By(5)通过电化学方法在具有两叶片的Votator型刮板式换热器中进行了传热相关性的实验研究。在铁氰化物/亚铁氰化物氧化还原电化学反应中在扩散控制下通过传质进行测量。传热相关性是从传热和传质的类比中获得的。通过改变旋转雷诺数,流体流量,普朗特数和当量直径来测量交换器外柱壁上的局部传热系数,以获得统一的热设计方程式。发现高普朗特数流体与下式相关:Nu = 1.53Rer0.51Pr0.33(Do / De)0.44(1320 Pr Do / De Rer和De分别是叶片旋转雷诺数和等效直径。

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