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Forced Convection Heat Transfer of Liquid-Gas Foam around a Circular Cylinder

Forced Convection Heat Transfer of Liquid-Gas Foam around a Circular Cylinder
液-气泡沫绕圆柱体的强制对流换热
批准号:
11650200
负责人:
TOKURA Ikuo
金额:
$0.7万
依托单位国家:
日本
项目类别:
Grant-in-Aid for Scientific Research (C)
财政年份:
1999
资助国家:
日本
项目状态:
已结题
起止时间:
1999 至 2000

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中文摘要
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英文摘要
Water-air foam is a new material for a coolant and expected to be applied in various industrial fields in the future. To clarify thermal properties of the flowing foam, forced convection heat transfer experiments were conducted by using a heated circular cylinder. Foam with wide rage of expansion ratio and various values of foam velocity was used in this study. We can draw the following conclusions from the study conducted in the academic years of 1999 and 2000.○When the temperature of the heating surface is less than 373K.The value of mean heat transfer coefficient for foam flow ranges between those for water and the air flows. This result suggest that intermediate cooling rate between water cooling and air cooling is obtained by using a liquid-gas foam. The heat transfer coefficient increases with increasing foam velocity and with decreasing the expansion ratio of the foam. It was indicated that the-value of the coefficient extremely decreases in a condition of low velocity and high … More expansion ratio of the foam. The heat transfer coefficient increases with the temperature difference between the heating surface and the foam. This result is much different from the heat transfer characteristics of usual one-phase fluids. Numerical analysis shows that the latent heat transfer by water vapor diffusion in the foam is the one of the important factors that increases the heat transfer coefficient at higher temperature range.○When the temperature increases over 373K.When the heat flux is increased gradually, the temperature of the heating surface increases and reaches 373K, i.e., the boiling point of water. Farther increase in the heat flux result in the temperature remains 373K for a while, and then begin to increase rapidly. The rate of increase in the heat flux with the surface temperature is relatively low in a super heated region. This boiling heat transfer characteristic of the foam flow is also much different from those for one phase liquids. In the temperature range around 373K, the heat flux for the foam flow is greater then that for water. In other temperature ranges, the heat flux for foam flow is lower than that of water. Less
期刊论文(3)
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会议论文
T.Matuda, I.Tokura, N.Ogawa and S.Ogahata: "Pressure Drop and Heat Transfer for Foam Flow Through a Circular Pipe"Pre-prints of Fluid Engineering Conference 2000, JSME. No.00-14. 150 (2000)
T.Matuda、I.Tokura、N.Okawa 和 S.Ogahata:“通过圆形管道的泡沫流的压降和传热”2000 年流体工程会议预印本,JSME。
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通讯作者:
戸倉郁夫 ほか3名: "流動液体泡沫の加熱円筒回りの熱伝達"日本機械学会北海道支部第40回講演会講演概要集. No.002-1. 142-143 (2000)
Ikuo Tokura 等 3 人:“流动液体泡沫加热筒周围的传热”日本机械工程师学会第 40 届北海道分会摘要第 002-143 号(2000 年)。
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通讯作者:
I,Tokura, et al.: "Heat Tranfer Characteristics of Foam Flow at Temperature up to 373K"Proceedings of 4th JSME-KSME Thermal Engineering Conference. Vol.3. 45-50 (2000)
I,Tokura, et al.:“泡沫流在温度高达 373K 时的传热特性”第四届 JSME-KSME 热工会议论文集。
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A Study on Pressure Drop for Liquid-Gas Foam through Channels
  • 批准号:
    08650185
  • 项目类别:
    Grant-in-Aid for Scientific Research (C)
  • 资助金额:
    $0.19万
  • 财政年份:
    1996
  • 负责人:
    TOKURA Ikuo
  • 依托单位:
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