Experimental investigation on the influence of lubricant oil on CO2 nucleate pool boiling heat transfer characteristics

• Published in: Applied thermal engineering 2025-02, Vol.260, p.124975, Article 124975
• Main Authors: Huang, Yongfang, Xu, Xiaoxiao, Luo, MingWen, Dang, Chaobin
• Format: Article
• Language: English
• Subjects: Boiling heat transfer; CO2; Lubricant oil; Nucleate pool boiling; Refrigerant/oil mixtures
• ISSN: 1359-4311
• DOI: 10.1016/j.applthermaleng.2024.124975

•The evaporation temperature has less effect on CO2 nucleate boiling heat transfer.•Oil addition leads to a higher nucleation site density and a smaller bubble diameter.•Mixtures boiling depends on the rates of oil deposition and refrigerant evaporation. As a natural working fluid, CO2 is considered the most promising alternative refrigerant to hydrofluorocarbons. In the fields of automotive air conditioning and commercial heat pumps, transcritical CO2 cycles show significant potential for performance enhancement. Although there are many studies on CO2 flow boiling in the open literature, few studies involve CO2 nucleate boiling heat transfer, which is the dominant mechanism of CO2 flow boiling heat transfer process. This study is proposed to conduct experimental investigations of CO2 nucleate boiling heat transfer. The influences of evaporation temperature, heat flux and lubricant oil addition on boiling heat transfer performance and bubble dynamic characteristics are discussed. The results show that in pure CO2 nucleate boiling, heat flux increase leads to higher bubble density and bubble diameter in bulk liquid, which in turn enhances boiling heat transfer. The effect of evaporation temperature increases on bubble diameter is significant. The reduction in bubble diameter weakens the convective heat transfer caused by bubble motion, which leads to less variation in the CO2 nucleate boiling heat transfer coefficient with evaporation temperature. Lubricant oil addition significantly changes the bubble dynamics of CO2 nucleate boiling process, leading to larger bubble density and smaller bubble diameter. Moreover, the oil diffusion at the phase interface notably affects the heat transfer performance, resulting in greater differences in the boiling heat transfer characteristics of the mixtures compared to that of pure CO2. The mixture boiling heat transfer coefficient is collectively influenced by evaporation temperature, heat flux and oil concentration. The experimental results suggest that the heat transfer coefficient of the mixture with an oil concentration of 0.5 % increases by an average of 25 % compared to pure CO2 at an evaporation temperature of 0 °C. At higher evaporation temperatures and high oil concentrations (>1%), oil addition leads to heat transfer deterioration. Findings from this work can provide a better understanding of oil effect on refrigerant boiling heat transfer and a fundamental basis for heat exchanger design of CO2 systems.