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首页> 外文期刊>Numerical Heat Transfer, Part A: Applications >Laminar Natural Convection of Bingham Fluids in a Square Enclosure with Vertical Walls Subjected to Constant Heat Flux
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Laminar Natural Convection of Bingham Fluids in a Square Enclosure with Vertical Walls Subjected to Constant Heat Flux

机译:恒热流作用下方形壁式方形外壳中宾汉流体的层流自然对流

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In this study, two-dimensional steady-state simulations of laminar natural convection in square enclosures with vertical sidewalls subjected to constant heat flux have been carried out, where the enclosures are considered to be completely filled with a yield-stress fluid obeying the Bingham model. Yield stress effects on heat and momentum transport are investigated for nominal values of Rayleigh number (Ra) in the range 103-106 and a Prandtl number (Pr) range of 0.1-100. It is found that the mean Nusselt number Nu increases with increasing values of Rayleigh number for both Newtonian and Bingham fluids. However, Nu values obtained for Bingham fluids are smaller than that obtained in the case of Newtonian fluids with the same nominal value of Rayleigh number Ra due to weakening of convective transport. The mean Nusselt number Nu in the case of Bingham fluids is found to decrease with increasing Bingham number, and for large values of Bingham number Bn, the value settles to unity (Nu = 1.0) as heat transfer takes place principally due to thermal conduction. The Nu values for the vertical walls subjected to constant heat flux are smaller than the corresponding values in the same configuration with constant vertical wall temperatures (for identical values of nominal Rayleigh, Prandtl, and Bingham numbers). However, the value of Bingham number at which Nu approaches to unity remains the same for both constant wall temperature and constant wall heat flux configurations. It is demonstrated that for small values of Bingham number Nu increases with increasing Prandtl number, but the opposite behavior occurs for large values of Bingham number. New correlations are proposed for the mean Nusselt number Nu for both Newtonian and Bingham fluids for square enclosures with vertical walls subjected to constant heat flux, which are shown to satisfactorily capture the correct qualitative and quantitative behavior of Nu in response to changes in Ra, Pr, and Bn.View full textDownload full textRelated var addthis_config = { ui_cobrand: "Taylor & Francis Online", services_compact: "citeulike,netvibes,twitter,technorati,delicious,linkedin,facebook,stumbleupon,digg,google,more", pubid: "ra-4dff56cd6bb1830b" }; Add to shortlist Link Permalink http://dx.doi.org/10.1080/10407782.2011.594417
机译:在这项研究中,已经进行了垂直侧壁受到恒定热通量的方形围护结构中层流自然对流的二维稳态模拟,其中该围护结构被认为完全服从了Bingham模型,并充满了屈服应力流体。 。研究了瑞利数(Ra)标称值在10 3 -10 6 和Prandtl数(Pr)范围为10的名义应力对热量和动量传输的影响。 0.1-100。发现牛顿流体和宾厄姆流体的平均努塞尔数Nu随瑞利数值的增加而增加。但是,由于对流输运减弱,对于宾汉流体获得的Nu值小于在具有相同瑞利数Ra标称值的牛顿流体的情况下获得的Nu值。发现在宾厄姆流体的情况下,平均努塞尔数Nu随宾厄姆数的增加而减小,并且对于宾厄姆数Bn的较大值,该值稳定为单位(Nu = 1.0),因为传热主要是由于热传导引起的。经受恒定热通量的垂直壁的Nu值小于垂直壁温度恒定的相同配置下的相应Nu值(对于标称瑞利,普朗特和宾汉姆数相同的值)。但是,对于恒定的壁温和恒定的壁热通量配置,Nu接近于1的Bingham数的值保持相同。已经证明,对于较小的宾厄姆数,Nu随着普朗特数的增加而增加,但是对于较大的宾厄姆数,则发生相反的行为。对于具有恒定热通量的垂直壁的方形围墙,牛顿流体和宾汉流体的平均努素数Nu提出了新的相关性,这些相关性被证明可以令人满意地捕获Nu的正确定性和定量行为,以响应Ra,Pr的变化和Bn。查看全文下载全文相关变量var addthis_config = {ui_cobrand:“泰勒和弗朗西斯在线”,servicescompact:“ citeulike,netvibes,twitter,technorati,delicious,linkedin,facebook,stumbleupon,digg,google,更多”,pubid: “ ra-4dff56cd6bb1830b”};添加到候选列表链接永久链接http://dx.doi.org/10.1080/10407782.2011.594417

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