Research on Heat and Mass Transfer Performance of Copper Foam Condensation Dehumidification Core for Space Station
|更新时间:2025-01-15
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Research on Heat and Mass Transfer Performance of Copper Foam Condensation Dehumidification Core for Space Station
Journal of Refrigeration(2025)
作者机构:
上海理工大学
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Research on Heat and Mass Transfer Performance of Copper Foam Condensation Dehumidification Core for Space Station[J/OL]. Journal of Refrigeration, 2025.
DOI:
Research on Heat and Mass Transfer Performance of Copper Foam Condensation Dehumidification Core for Space Station[J/OL]. Journal of Refrigeration, 2025.DOI:
Research on Heat and Mass Transfer Performance of Copper Foam Condensation Dehumidification Core for Space Station
To address the demands for high-efficiency heat transfer and compact lightweight design in space stations
a high-efficiency condensation dehumidification system utilizing copper foam and driven by a Stirling refrigerator was developed. An experimental study was conducted to investigate its heat and mass transfer characteristics under various conditions. The experimental parameters were set as follows: air inlet temperature ranging from 20 to 30 °C
relative humidity between 50 % and 80 %
cold plate temperature from 8 to 13 °C
and inlet wind speed from 0.4 to 1.4 m/s. The results indicate a positive correlation between the increase in air inlet temperature and the enhancement of both heat transfer coefficient and mass transfer coefficient. Specifically
when the air inlet temperature increased from 20 °C to 30 °C
the heat transfer coefficient rose by 10.5 %
while the mass transfer coefficient exhibited a more substantial increase of 57.1 %. Furthermore
variations in the relative humidity of the air inlet had distinct impacts on the heat and mass transfer coefficients: the heat transfer coefficient decreased with increasing relative humidity
whereas the mass transfer coefficient increased. Notably
although lowering the cold plate temperature can significantly improve heat transfer
it concurrently diminishes the efficiency of heat and mass transfer. Therefore
selecting an appropriate cold plate temperature is crucial. Additionally
the efficiency of heat and mass transfer was markedly enhanced with increasing inlet wind speed; however
a continuous increase in wind speed resulted in higher system energy consumption. Thus
a balance between achieving efficient heat transfer and managing system energy consumption is essential. Based on extensive experimental data
the heat transfer model was refined through regression analysis. The relative average deviation between theoretical and experimental values was found to be 8.97 %
with a relative standard deviation of 8.21 %
demonstrating the model's strong predictive accuracy.