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Evolution of natural convection melting inside cavity heated from different sides using enthalpy based lattice Boltzmann method

机译:基于焓的格子玻尔兹曼方法从不同侧面加热腔体内自然对流熔化的演变

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摘要

Melting coupled with natural convection in cavity has always been a hot topic. In this paper, natural convection melting in cavity heated from different sides are numerically simulated using the enthalpy based lattice Boltzmann method. The cavity model of one heated side and three adiabatic sides is employed to achieve totally melting. The dimensionless numbers are:Pr = 0.02,St = 0.01,Ra = 25,000 andRa = 50,000. Melting when heated from top is conduction melting, melting when heated from right is omitted due to its symmetry with the case when heated from left. The heat transfer and flow characteristics when heated from left and bottom are mainly investigated. Results indicate that, when heated from left and bottom, the melted region always enlarges but the growth of flow velocity is suppressed. In the final stage of melting, the temperature distribution tends to be uniform and the flow inside cavity gradually vanishes. Moreover, the melting efficiency when heated from bottom is significantly decreased by its first stage of conduction melting. AsRaincreases, that stage is obviously shortened, the melting efficiency is promoted rapidly. And the melting efficiency when heated from bottom exceeds the efficiency when heated from left at aroundRa = 25,000. Besides, melting from different sides are actually the problems of different angles between the heat flux out of the boundary and gravity. The effect of more different angles on the melting efficiency is further discussed. As the angle increases, the average dimensionless velocity also increases. Natural convection inside the cavity becomes stronger, and the melting efficiency gets higher.
机译:空腔中的熔化和自然对流一直是一个热门话题。在本文中,使用基于焓的点阵玻尔兹曼方法对从不同侧面加热的型腔中的自然对流熔融进行了数值模拟。一个加热侧和三个绝热侧的型腔模型被用来实现完全熔化。无量纲数为:Pr = 0.02,St = 0.01,Ra = 25,000和Ra = 50,000。从顶部加热时的熔化是传导熔化,从右侧加热时的熔化由于与从左侧加热时的情况对称而被省略。主要研究了从左侧和底部加热时的传热和流动特性。结果表明,当从左到右加热时,熔化区域总是扩大,但流速的增长受到抑制。在熔化的最后阶段,温度分布趋于均匀,型腔内部的流动逐渐消失。而且,从底部加热时的熔化效率在其传导熔化的第一阶段显着降低。随着增加,该阶段明显缩短,熔融效率迅速提高。从底部加热时的熔化效率超过从左侧加热时的熔化效率,约为Ra = 25,000。此外,从不同侧面熔化实际上是边界外的热通量与重力之间存在不同角度的问题。进一步讨论了更多不同角度对熔化效率的影响。随着角度增加,平均无量纲速度也增加。腔体内的自然对流变得更强,熔化效率也更高。

著录项

  • 来源
  • 作者单位

    Key Laboratory of Thermo-Fluid Science and Engineering, Ministry of Education, Xi’an Jiaotong University;

    Key Laboratory of Thermo-Fluid Science and Engineering, Ministry of Education, Xi’an Jiaotong University;

    Key Laboratory of Thermo-Fluid Science and Engineering, Ministry of Education, Xi’an Jiaotong University;

    Key Laboratory of Thermo-Fluid Science and Engineering, Ministry of Education, Xi’an Jiaotong University;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Melting; Natural Convection; Lattice Boltzmann Method; Melting efficiency;

    机译:熔化;自然对流;格子玻尔兹曼法;熔化效率;

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