Theoretical model for subcooled upward flow boiling heat transfer and critical heat flux for an inclined downward heated surface

• Published in: International journal of heat and mass transfer Vol. 213; p. 124351
• Main Authors: Dong, Shichang, Gong, Shengjie, Zhang, Botao, Xiong, Zhenqin, Yuan, Yidan, Ma, Weimin
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 01.10.2023
• Subjects: Bubble interaction; Critical heat flux; Dry spot; Flow boiling; Inclined channel; Bubble interaction; Flow boiling; Critical heat flux; Inclined channel; Dry spot
• ISSN: 0017-9310; 1879-2189; 1879-2189
• DOI: 10.1016/j.ijheatmasstransfer.2023.124351

•A heat flux model based on probability analysis of bubbles’ interaction is developed.•The boiling crisis is indicated based on the development of irreversible dry spot.•The model well predicts the boiling curve and CHF.•The model can predict the pressure, inlet subcooling, flow mass flux and wall wettability effects on boiling curves and CHF.•The model can be applicated to the flow boiling in inclined downward heated channel. The in-vessel retention system and ex-vessel retention system are very important to the safety of nuclear power plants under severe accidents. While the success of such safety systems relies on well understanding the corresponding physical mechanisms of boiling heat transfer and critical heat flux (CHF). Challenges till remain in accurately predicting the subcooled flow boiling curve especially in the low-pressure and low-flow conditions due to its complex boiling phenomenon. The present study introduces a theoretical model to predict the boiling curve and critical heat flux for subcooled flow boiling in inclined downward heated rectangular channel. The proposed model well estimates the transition from forced convection, isolated bubble nucleate boiling to fully developed boiling regime by considering the growth and interaction of bubbles. Through probability analysis of bubbles’ interaction, the proportion of heat flux in different boiling regimes is determined. In addition, the flow boiling CHF is predicted based on the probability analysis of dry spots. The new model is validated by the subcooled flow boiling experiments with vertical single-side heated channel under low-pressure and low-flow conditions. The predicted boiling curves are consistent with experimental results corresponding to different thermal-hydraulic parameters, such as pressure, mass flux, inlet subcooling and wall wettability (hydrophilic and hydrophobic), and the prediction error of CHF is within ±15%. Furthermore, the inclination effect on CHF is validated by the subcooled flow boiling experiments in inclined channel with the inclination angle varying from 0° to 90°, which shows the good applicability of the developed model.