Abstract
The boiling flow and heat transfer performance of four different pin-fins in microchannels are investigated through visualization experiment research. Flow boiling visualization results have been conducted by using deionized water as working fluid with circulating under flow rates in the range of 0.25~9kg/h, with the inlet temperature as 30 ℃ and heating power as 126W. The experimental results show that the flow patterns in the channel are mist flow, annular flow, isolated bubble and no bubble. And the flow pattern corresponds to the pressure change. With the increase of Re, the pressure drop in the microchannel first increases rapidly, then decreases, and finally increases again. The change process of pressure drop corresponds to the bubble heat transfer process. The corresponding heat transfer processes include film boiling、transition from film boiling to nucleation boiling、nucleation boiling and single-phase convection. At the same time, the state of bubbles in the channel can correspond to the intensity and mode of heat transfer. The average surface temperature of the bottom plate decreases with the increase of Re. The average convective heat transfer coefficient increases, then decreases and increases again with the increase of Re. The twice increases are mainly due to liquid film evaporation and single-phase flow transition. The average convective heat transfer coefficient increases with the increase of heat flux. And in four different micro-fin shapes, the heat transfer effect of triangle fin array is the best, because the disturbance of triangle to fluid is the most intense. While in the nucleation boiling region, the convective heat transfer coefficient of triangle micro-fin arrays is the largest. At that stage, the bubbles in triangle micro fin array grow and separate more easily.When the Re is less than 130, the number of bubbles in the triangle micro array is great than that in the ellipse micro array, and the bubble departure diameter is the largest, as well. And the bubble growth time and bubble waiting time are the shortest. When Re is greater than 130, the number of bubbles in the channel is relatively small, and the nucleation boiling intensity decreases. When the Re continues to increase, there are few or no bubbles in the channel, which is close to the single-phase convection. Moreover, the pressure drop, bottom temperature and convective heat transfer coefficient of triangle micro fin array change most obviously. The results show that when Re increases from 30 to 125, the bottom temperature decreases by 41 ℃, the maximum convective heat transfer coefficient reaches 16800 w / m2 · ℃, and the maximum Nu is 10.
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Abbreviations
- a :
-
long axis of micro pin-fin(m)
- A :
-
whole heat transfer area (m2)
- A b :
-
heat transfer area of microchannel without micro pin-fin (m2)
- A fin :
-
heat transfer area of micro pin-fin (m2)
- b :
-
short axis of micro pin-fin(m)
- d w :
-
the bubble departure diameter(m)
- D :
-
equivalent diameter (m)
- h av :
-
the average heat transfer coefficient (W/(m2·K))
- H :
-
height of micro pin-fin heat sink (m)
- L :
-
length of micro pin-fin heat sink (m)
- L 1 :
-
length of the area occupied by the pin-fin in the heat sink (m)
- Nu :
-
Nusselt number
- P sL :
-
wetted perimeter of cross section of microchannel(m)
- ΔP :
-
pressure drop between inlet and outlet of micro pin-fin arrays (Pa)
- Q :
-
volume flow rate (m3/s)
- Re :
-
Reynolds number
- S D :
-
oblique distance of pin-fin (m)
- S L :
-
longitudinal distance of pin-fin (m)
- S T :
-
transverse distance of pin-fin (m)
- t g :
-
the bubble growth time(s)
- t w :
-
the bubble waiting time(s)
- T surf :
-
temperature of surface (℃)
- T f :
-
temperature of working fluid (℃)
- u :
-
velocity of fluid (m/s)
- W :
-
width of micro pin-fin heat sink (m)
- Λ :
-
coefficient of thermal conductivity (W/m·K )
- η :
-
efficiency of micro pin-fin
- Φ :
-
heat flux (kW/m2)
- υ :
-
viscosity of the working fluid (m2·s)
- b:
-
sidewall which not occupied by micro pin-fin arrays
- fin:
-
micro pin-fin array
- m:
-
mass
- max:
-
maximum
- min:
-
minimum
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Sun, R., Hua, J., Zhang, X. et al. Experimental study on the effect of shape on the boiling flow and heat transfer characteristics of different pin-fin microchannels. Heat Mass Transfer 57, 2081–2095 (2021). https://doi.org/10.1007/s00231-021-03092-z
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DOI: https://doi.org/10.1007/s00231-021-03092-z