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局部热源尺度对Rayleigh-Bénard对流中流态转变与传热特性的影响

INFLUENCE OF HEAT-SOURCE SIZE ON FLOW-REGIME TRANSITION AND HEAT TRANSFER IN RAYLEIGH-BÉNARD CONVECTION WITH LOCALIZED HEATING

  • 摘要: 本文采用直接数值模拟方法研究了二维方腔内底部中心局部加热、顶部恒温冷却条件下的Rayleigh-Bénard对流. 计算中固定普朗特数 Pr = 4.3 , 系统改变瑞利数 Ra 和无量纲热源尺寸 \Lambda , 重点分析流动结构演化、偏转建立时间、平均流动强度及热源区域平均传热特性的变化规律. 基于平均角动量 L\left(t\right) 的时间演化分析, 研究将系统流动定量划分为近对称弱环流、稳定偏转环流和非定常反转环流三类典型状态, 并构建了参数空间中的流态分区. 结果表明, 随着 Ra 或 \Lambda 增大, 底部受热区的不稳定性增强, 系统逐渐由近对称弱环流向稳定偏转环流和非定常反转环流过渡, 且增大热源尺寸会使流态转变区域整体向较低 Ra 移动. 流动发生偏转的特征时间 \tau _rev 随 Ra 和 \Lambda 增大而整体缩短, 且反转状态的时间尺度对控制参数更为敏感. 在统计稳定阶段, 平均雷诺数 Re 和加热区域平均努塞尔数 Nu_h 均随 Ra 与 \Lambda 增大而增加, 且不同流态下 Re 数(或 Nu_h 数)与 Ra 数(或 \Lambda )的经验指数比较接近. 与经典全底板加热Rayleigh-Bénard对流相比, 局部加热下 Re 关于 Ra 的经验指数略高于1/2参考值, 而 Nu_h 关于 Ra 的经验指数相对较低; 随着 \Lambda 增大, 传热表现逐渐向全底板加热情形靠近.

     

    Abstract: Direct numerical simulations are performed to investigate Rayleigh-Bénard convection in a two-dimensional square cavity with localized heating at the center of the bottom wall and isothermal cooling at the top wall. The Prandtl number is fixed at Pr = 4.3 , while the Rayleigh number Ra and the dimensionless heat-source size \Lambda are systematically varied over a prescribed parameter range. The evolution of flow structures, the deflection-establishment time, the mean flow strength, and the heat-source-averaged heat-transfer characteristics under localized heating are analyzed. Based on the temporal evolution of the mean angular momentum L\left(t\right) , the flow is quantitatively classified into three typical regimes: near-symmetric weak circulation, stable deflected circulation, and nonstationary reversal circulation. A complete regime map in the \left(\Lambda ,Ra\right) parameter space is then constructed. The results show that, as Ra or \Lambda increases, the driving effect of the bottom thermal plume is enhanced, and the system gradually transitions from near-symmetric weak circulation to stable deflected circulation and nonstationary reversal circulation. Increasing the heat-source size shifts the regime-transition region toward lower Ra . The characteristic time for flow deflection, \tau _rev , decreases overall with increasing Ra and \Lambda , and the time scale in the reversal regime is more sensitive to the control parameters. In the statistically steady stage, both the mean Reynolds number Re and the heat-source-averaged Nusselt number Nu_h increase with Ra and \Lambda . The empirical exponents of Re or Nu_h with respect to Ra or \Lambda are close among different flow regimes. Compared with classical Rayleigh-Bénard convection with full-bottom heating, the locally heated system exhibits a slightly larger empirical exponent of Re with respect to Ra than the 1/2 reference value, whereas the empirical exponent of Nu_h with respect to Ra is relatively lower. As the heat-source size \Lambda increases, this localized-heating effect is gradually weakened, and the heat-transfer behavior progressively approaches that of the full-bottom-heating case. These results provide a reference for understanding the coupling between localized thermal forcing, flow-regime transition, and heat transport in confined convection systems.

     

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