翅片结构对超汽化结构换热性能影响的研究

基于计算流体动力学软件ANSYS CFX,利用非均相流欧拉-欧拉模型耦合RPI(伦斯勒理工大学)沸腾模型开展超汽化冷却结构的过冷沸腾两相流模拟,比较不同翅片结构对超汽化结构换热性能的影响。研究发现在高热流量条件下三角形翅片结构的换热性能优于矩形翅片结构:其中顺流4×3三角形翅片结构总体换热性能最好;矩形4×3翅片结构受流速影响较大,由于翅片的阻碍作用使得流速越来越低,换热性能越来越差;逆流4×3三角形翅片结构由于其翅片间的腔小,并且逆流翅片对主流的破坏使得腔内流体保持着很大的湍度,所以翅片区有很好的换热性能,但由于逆流翅片对流体阻碍作用大,小槽内流体速度越来越低,使得远离翅片区的侧边换热性能逐渐变差。

Study on the effect of fin structure on heat transfer performance of hypervapotron structure

Based on the computational fluid dynamic code ANSYS CFX, the inhomogeneous Eulerian- Eulerian multiphase model coupled with RPI (Rensselaer Polytechnic Institute) boiling model is adopted to simulate the subcooled boiling two-phase flow of hypervapotron structure, and the effects of different fin structures on the heat transfer performance of hypervapotron structures are compared. The results show that under high heat flux conditions, the heat transfer performance of the triangular fin structure is better than the rectangular fin structure. Triangular 4×3 to the flow geometry has the best heat transfer performance. Rectangular 4×3 geometry is greatly affected by the flow rate due to the obstruction of the fins making the flow rate to be lower and the heat transfer performance will be getting worse. Triangular 4×3 against the flow geometry make the fluid in the cavity to maintain a large degree of turbulence due to the small cavity between the fins and the adverse effects of counter-flow fins on the mainstream, so the fin area has a good heat transfer performance, but due to the impeding effect of the counter-flow fin on the fluid, the fluid velocity in the slot is getting lower and lower, as the result, the heat transfer performance on the sidewall far away from the fin area is getting worse.