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Three-dimensional numerical simulation of natural convection in an inclined liquid-filled enclosure with an array of discrete heaters

机译:带有离散加热器阵列的倾斜液体填充外壳中自然对流的三维数值模拟

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摘要

A three-dimensional (3-D) numerical model is developed to investigate the effects of inclination on the heat transport processes in a liquid-filled rectangular enclosure of finite size. The interactions of flows tangential and normal to the heater surfaces in an inclined enclosure cause a slight oscillation in Nusselt number. Inclination has little effects on the average heat transfer characteristics except configurations close to the conduction case with heaters on top leading to a sharp decrease in Nusselt number. The critical Rayleigh number of 1708 is also observed in the present study regardless of inclinations. Heat transfer from discrete heaters is non-uniform. Maximum Nusselt number occurs at the heater leading edge and decreases towards the trailing edge. Correlations for the row average Nusselt number vs. Rayleigh number at various inclination angles are presented. By taking the average of the discrete heater array, the numerical results compared well with the. empirical correlations obtained from a single heater plate in literature.
机译:建立了三维(3-D)数值模型,以研究倾角对有限尺寸的液体填充矩形外壳中传热过程的影响。在倾斜的外壳中,切向流和垂直于加热器表面的流的相互作用会导致Nusselt数的轻微波动。倾斜度对平均传热特性的影响很小,除了接近导热箱的结构(加热器位于顶部)会导致Nusselt数急剧下降。无论倾斜度如何,在本研究中也观察到了临界瑞利数1708。分立加热器的传热不均匀。最大努塞尔数出现在加热器的前缘,并朝后缘减小。给出了在各种倾斜角度下行平均努塞尔数与瑞利数的相关性。通过取离散加热器阵列的平均值,数值结果与之比较。从文献中的单个加热板获得的经验相关性。

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