环状流道内层流化现象的研究:第2报内菅加热的情况

鳥居 修一, 清水 昭比古, 修 長谷川
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引用次数: 0

摘要

为了弄清湍流向层流反转的发生条件,对环形通道内的对流换热进行了实验研究。检测的雷诺数范围从6000到10000,无量纲加热参数q^+_m从0.2×10^到4.5×10^。虽然在无量纲加热参数方面,大多数实验条件满足目前提出的圆管流动标准,但在本研究中没有观察到明确的分层现象。而在加热充分发展的区域,Nusselt数与众所周知的变流性传热相关关系最大下降10%,与S. Fuji等人提出的相关关系相当一致。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
環状流路内の層流化現象に関する研究 : 第2報 内菅加熱の場合
Experimental study was performed on convective heat transfer in annular passage in order to clarify the condition for occurrence of turbulent to laminar reverse transition. Examined Reynolds number ranged from 6000 to 10000 and nondimensional heating parameter q^+_m from 0.2×10^ to 4.5×10^ . Although most of experimental conditions in terms of nondimensional heating parameter satisfied the criteria proposed so far for circular tube flows, no definite laminarization was observed in the present study. At the region of fully developed heating, however, Nusselt number shows maximum 10% drop from the well known heat transfer correlation of variable flow properties, and rather agrees with the correlation proposed by S. Fuji et al.
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