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Heat transfer and crisis phenomena at pool boiling of liquid nitrogen on the surfaces with capillary-porous coatings

机译:带有毛细孔涂层的液氮在表面沸腾时的传热和危机现象

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The results of experimental study of heat transfer and crisis phenomena at pool boiling of liquid nitrogen with different heating conditions on the surface with capillary-porous coating are presented. Porous coatings with different thicknesses (400 and 1390 urn), morphology and high porosity (up to 80%) were obtained using the new plasma spraying technique. It was shown that at steady-state heat release the heat transfer at boiling essentially depends on the thickness and morphology of the coating. The maximum enhancement (~300%) compared to the smooth heater was detected to coated heater with a thickness of 1390 μm at low heat fluxes. The mechanism of heat transfer enhancement at pool boiling by using the capillary-porous coatings was proposed. Heat transfer hysteresis was detected for the heater with the coating of 400 μm. For the smooth heaters and the heater with 1390 μm coating, the heat transfer coefficients almost coincide with an increase in the heat flux and with its decrease. Data on the effect of coatings with different thicknesses on the critical heat flux (CHF) at boiling under steady-state heat release are presented. It is shown that for the smooth heaters the value of critical heat flux at rapid heating decreases in comparison with steady-state heat release. Capillary-porous coatings have a significant influence on development of the transition process and crisis phenomena at stepwise heat release. There is degeneration of boiling crisis development at rapid heating on the coated surfaces at the heat fluxes below the value of the CHF at steady state heat release. Fast transition to film boiling at stepwise heat release on the coated heaters with different thicknesses is observed at the heat fluxes 2 times higher than the critical heat fluxes, obtained at steady state heating.
机译:提出了在不同温度条件下毛细孔涂层表面液氮池沸腾过程中传热和危机现象的实验研究结果。使用新的等离子喷涂技术可以获得具有不同厚度(400和1390 um),形态和高孔隙率(高达80%)的多孔涂层。结果表明,在稳态释放热量时,沸腾时的传热基本上取决于涂层的厚度和形态。在低热通量下,相对于厚度为1390μm的涂层加热器,检测到与光滑加热器相比最大的增强(〜300%)。提出了利用毛细孔涂层促进池沸腾传热的机理。检测到涂层厚度为400μm的加热器的传热滞后。对于平整型加热器和涂层为1390μm的加热器,传热系数几乎与热通量的增加和减少一致。给出了不同厚度的涂层对稳态热释放下沸腾时的临界热通量(CHF)的影响的数据。结果表明,对于光滑加热器,与稳态放热相比,快速加热时的临界热通量值降低。毛细管多孔涂层对过渡过程的发展和逐步放热时的危机现象有重大影响。在稳态热释放下,在热流以下低于CHF值的情况下,在涂层表面上快速加热时,沸腾危机的发展会恶化。在稳态加热下获得的临界热通量高出2倍的热通量下,在具有不同厚度的涂层加热器上逐步释放热量后,薄膜迅速沸腾。

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