Heat transfer characteristics of wettability gradient surfaces in spray cooling
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摘要:
采用组分输运模型discrete phase model(DPM)和欧拉壁面液膜模型对加热条件下圆环形化学图案改性表面上的喷雾冷却流动换热特性进行了数值模拟。通过对比四种改性表面的液膜厚度、液膜流速、表面温度不均匀性和平均表面传热系数的变化研究了润湿性梯度对表面流动换热特性的影响。结果表明:润湿性梯度表面的换热性能优于均匀润湿性表面,可以促进排液,优化液体管理。润湿性梯度大的表面,液膜流速快、液膜厚度小,疏水表面的排液效果可能优于亲-疏水混合表面,但通过疏水促进成核和亲水延缓干涸的良好设计,亲-疏水混合表面的换热性能最好,并且能够改善表面温度不均匀性。增加润湿性数量和增大梯度,可强化换热。
Abstract:The Species Transport model, Discrete Phase Model (DPM) and Eulerian wall film model were used to simulate the heat transfer characteristics of the spray cooling on circular chemically patterned modified surfaces under uniform heating conditions. The effect of wettability gradient on heat transfer performance on surfaces was studied by comparing four modified surfaces’ liquid film thickness, liquid film flow rate, surface temperature inhomogeneity and average surface heat transfer coefficient. The results showed that the heat transfer performance of the wettability gradient surfaces was better than that of uniformly wet table surfaces, which can promote the liquid drainage and optimize the liquid management. Surfaces with large wettability gradients had faster liquid film flow rate and smaller liquid film thickness, and hydrophobic surfaces may have better liquid drainage than hydrophilic-hydrophobic hybrid surfaces, yet hydrophilic-hydrophobic hybrid surfaces had the best heat transfer performance through a good hydrophobic design to promote nucleation and hydrophilic performance to retard drying, and can improve surface temperature inhomogeneity. Increasing the number of wettability and increasing the gradient can enhance the heat transfer.
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Key words:
- spray cooling /
- modified surfaces /
- wettability gradient /
- liquid drainage /
- heat transfer
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表 1 不同模拟工况的边界条件
Table 1. Boundary conditions for different simulation conditions
喷雾
压力/Pa喷雾
高度/mm热流密度/
(W/cm2)数量/个 表面类型 接触角 外圆环$ {\theta }_{1} $/ (°) 中圆环$ {\theta }_{2} $/ (°) 内圆环$ {\theta }_{3} $/ (°) 1000000 10 100 1 超亲水[18] 10 10 10 亲水 50 50 50 铜基[19] 88 88 88 分界[18] 90 90 90 疏水 120 120 120 超疏水[18] 150 150 150 2 亲水 10 10 50 疏水 120 120 150 亲-疏水混合 50 50 120 10 10 150 3 亲水 10 50 90 疏水 90 120 150 亲-疏水混合 50 90 120 10 90 150 表 2 模拟参数
Table 2. simulation parameters
工质 质量流量/ (L/min) 喷射半锥角/ (°) 喷嘴直径/ mm 初始液膜厚度/ mm 水 0.52 30 0.56 0.03 -
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