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Numerical model for non-equilibrium heat and mass exchange in conjugate fluid/solid/porous domains with application to evaporative cooling and drying

机译:共轭流体/固体/多孔区域内非平衡热质交换的数值模型及其在蒸发冷却和干燥中的应用

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摘要

A numerical formulation capable of simulating fluid flow and non-equilibrium heat and mass transfer in three-dimensional conjugate fluid/solid/porous domains is presented. The governing transport equations are presented for the fluid, solid, and porous regions, with special consideration given towards the manner in which moisture is accounted for in the air-water vapour mixture. Mathematical conditions are also presented to ensure that heat and mass transfer occurs smoothly across fluid-porous, fluid-solid and porous-solid interfaces. The developed formulation is validated by simulating direct and indirect evaporative cooling problems. The results demonstrate that the formulation is capable of simulating evaporative cooling in conjugate three-dimensional domains, with and without the addition of sensible heat. Moreover, different simulated cases show that the results are accurate compared to available experimental results, and are physically realistic throughout the domain and at interfaces between conjugate regions. The unsteady problem of drying of an initially saturated porous material is also simulated to demonstrate the non-equilibrium mass transfer feature of the developed formulation. The results show the correct trends in drying time with respect to the flow Reynolds number and the relative humidity of the inlet air-water vapour mixture.
机译:提出了一种能够在三维共轭流体/固体/多孔域中模拟流体流动以及非平衡传热和传质的数值公式。给出了流体,固体和多孔区域的控制输运方程,并特别考虑了在空气-水蒸气混合物中考虑水分的方式。还提出了数学条件,以确保在流体-多孔,流体-固体和多孔-固体界面之间顺利进行传热和传质。通过模拟直接和间接蒸发冷却问题验证了开发的配方。结果表明,该配方能够模拟共轭三维域中的蒸发冷却,而无需添加显热。此外,不同的模拟情况表明,与可用的实验结果相比,结果是准确的,并且在整个域中以及共轭区域之间的界面处在物理上都是现实的。还模拟了最初饱和的多孔材料干燥的不稳定问题,以证明所开发配方的非平衡传质特性。结果表明干燥时间相对于流动雷诺数和进气空气-水蒸气混合物的相对湿度的正确趋势。

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