Effect of flow direction on heat transfer characteristics of supercritical CO2 in a heating serpentine micro-tube

被引:23
作者
Xu, Yong [1 ,2 ]
Yi, Zhengming [1 ,2 ]
机构
[1] Wuhan Univ Sci & Technol, State Key Lab Refractories & Met, Wuhan 430081, Peoples R China
[2] Wuhan Univ Sci & Technol, Key Lab Ferrous Met & Resources Utilizat, Minist Educ, Wuhan 430081, Peoples R China
基金
中国国家自然科学基金;
关键词
Heating heat transfer; Serpentine micro -tube; Buoyancy effect; Centrifugal force; SupercriticalCO2; HELICALLY COILED TUBE; VERTICAL MINI-TUBE; CARBON-DIOXIDE; BUOYANCY FORCE; PRESSURE-DROP; CONVECTION;
D O I
10.1016/j.energy.2022.125474
中图分类号
O414.1 [热力学];
学科分类号
摘要
The combined effect of gravitational buoyancy, centrifugal force and centrifugal buoyancy on the heat transfer of supercritical CO2 in a serpentine micro-tube under different flow directions is numerically studied. The comprehensive heat transfer performance in the four flow directions is vertical upward flow (VU), horizontal flow vertical bend (HV), horizontal flow horizontal bend (HH) and vertical downward flow (VD) in ascending order. Considering the angle between gravity and centrifugal force and the angle between gravity and local flow direction, Richardson number can better reflect the effect degree of buoyancy under different flow directions. In VU, VD and HV, the gravitational buoyancy at low mass flux can weaken the local heat transfer deterioration at the turning point, but the gravitational buoyancy at high mass flux can only weaken the local heat transfer deterioration at the turning point when the heat transfer of tube section is enhanced. In HH, the local flow di-rection, gravity and centrifugal force are perpendicular to each other, and the location of local heat transfer deterioration at the turning point is affected by the ratio of centrifugal force to gravity.
引用
收藏
页数:14
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