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Forced convection heat transfer with water and phase-change-material slurries: Turbulent flow in a circular tube.

机译:与水和相变材料浆料的强制对流换热:圆管中的湍流。

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摘要

The objective of the present study was to understand the fundamental mechanism of the enhancement of the convective heat transfer coefficient as well as the thermal capacity of a working fluid by using the latent heat of the solid-liquid phase change of particles.; Tests were performed with water flowing turbulently in a long heating test section (i.e., 627 diameters) with a uniform heat flux boundary condition. Three effects influence the local friction and heat transfer coefficients: (1) the developing effect, (2) the radial viscosity change effect, and (3) the axial viscosity change effect. A new analysis method to obtain fully developed friction factor and Nusselt number is proposed. The Blasius equation, f = 0.079 Re{dollar}sp{lcub}-0.25{rcub},{dollar} was found to yield a good prediction of the turbulent friction coefficient with a 2.1% error. It would make a better prediction if the proportionality constant 0.079 in the equation was replaced with a new constant: 0.081. The power factor, m, in a general Nusselt number correlation, Nu = C Re{dollar}sp{lcub}rm m{rcub}{dollar} Pr{dollar}sp{lcub}0.4{rcub},{dollar} was found to be 0.979, which was greater than the widely used value of 0.8 used in the Dittus-Boelter correlation.; Tests were also conducted with a phase-change-material (PCM) slurry that was a suspension of PCM particles in a carrier fluid, water. A new method to generate very fine PCM particles using an emulsifier was introduced. With such fine PCM particles, the flow loop did not clog. Local pressure drops and local heat transfer coefficients were measured along the test section. Significant decreases in pressure drop occurred where the PCM particles in the slurry melted. The local convective heat transfer coefficient was found to vary significantly (up to 200%) when the particles melted. This made it difficult to directly apply the LMTD method or the effective thermal capacity method, which had been used in previous researches, to the heat transfer analysis of the PCM slurry flow. A new three-region melting model is proposed, and an explanation of the physical mechanism of the convective heat transfer enhancement due to the PCM particles is provided.
机译:本研究的目的是通过利用颗粒的固液相变潜热来了解提高对流传热系数以及工作流体的热容量的基本机理。在均匀的热通量边界条件下,在长加热试验段(即627直径)中湍流流动的水进行试验。三个因素影响局部摩擦系数和传热系数:(1)显影效应;(2)径向粘度变化效应;(3)轴向粘度变化效应。提出了一种获得充分发展的摩擦系数和努塞尔特数的新分析方法。发现Blasius方程f = 0.079 Re {dollar} sp {lcub} -0.25 {rcub},{dollar}可以很好地预测湍流摩擦系数,误差为2.1%。如果将方程中的比例常数0.079替换为新的常数0.081,将会做出更好的预测。在一般的努塞尔特数相关中,功率因数m = N Re =(Re)为0.979,大于Dittus-Boelter相关中使用的0.8的广泛使用值。还对相变材料(PCM)浆液进行了测试,该相变材料浆液是PCM颗粒在载流体水中的悬浮液。介绍了一种使用乳化剂产生非常细的PCM颗粒的新方法。使用如此细的PCM颗粒,流动环路不会阻塞。沿测试部分测量局部压降和局部传热系数。浆料中的PCM颗粒熔化时,压降显着降低。发现当颗粒熔化时,局部对流传热系数发生显着变化(高达200%)。这使得难以将先前研究中使用的LMTD方法或有效热容方法直接应用于PCM浆料流的传热分析。提出了一种新的三区域熔化模型,并解释了由于PCM颗粒引起的对流传热增强的物理机理。

著录项

  • 作者

    Choi, Eunsoo.;

  • 作者单位

    Drexel University.;

  • 授予单位 Drexel University.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 1993
  • 页码 149 p.
  • 总页数 149
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 机械、仪表工业;
  • 关键词

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