Abstract
In the present study, the pool boiling process for the refrigerant R141b and its mixtures with Span 80 surfactant and TiO2 nanoparticles has been examined. The results for the heat transfer coefficient (HTC) were taken at various boiling pressures (0.2, 0.3, 0.4 MPa) in the range of the heat fluxes 5.8–56.4 kW m−2 and for the internal boiling characteristics (IBC) such as the bubble departure diameter, frequency and velocity of bubble growth at atmospheric pressure in the range of the heat fluxes 29.6–57.0 kW m−2. We found that the additives of Span 80 and Span 80/TiO2 nanoparticles enhance the HTC at the lower heat flux densities and pressures. However, at higher values of the heat flux and pressure the HTC was deteriorated by the additives. At the same time, no significant impact was obtained for the IBCs. An analysis of the Rensselaer Polytechnic Institute model performance for the case when experimental data on the nucleation sites density is unavailable has revealed no qualitative agreement between experimental and predicted data on the HTC. Thus, we proposed a new approach that combines limited set of the experimental data (LSED) with correlations of the IBC’s versus heat flux and pressure. Finally, the LSED allowed to achieve both qualitative and quantitative agreement (within ± 10%) between predicted and experimental data on the HTC.
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Abbreviations
- A, B, C :
-
Empirical coefficients
- A :
-
Surface area of the heater (m2)
- \(\bar{d}_{\text{b}}\) :
-
Mean bubble departure diameter (mm)
- \(d_{\text{h}}\) :
-
Diameter of heating surface (m)
- \(\bar{f}_{\text{b}}\) :
-
Mean bubble departure frequency (s−1)
- h :
-
Heat transfer coefficient (kW m−2 K−1)
- k :
-
Thermal conductivity (W m−1 K−1)
- \(n_{\text{b}}\) :
-
Nucleation site density (m−2)
- P :
-
Pressure (MPa)
- q :
-
Heat flux density (kW m−2)
- Q :
-
Heat flux (kW)
- r mean :
-
Mean equivalent radius of nanoparticles in nanofluid (nm)
- R rc :
-
Resistance of resistance coil (Ω)
- T :
-
Temperature (K)
- U h :
-
Voltage drop across the heater (V)
- U rc :
-
Voltage drop across the resistance coil (V)
- \(\bar{w}_{\text{b}}\) :
-
Mean velocity of bubble growth (mm s−1)
- \(\Delta h\) :
-
Heat of vaporization (J kg−1)
- \(\Delta T\) :
-
Wall superheat, \(T_{\text{S}} - T_{\text{w}}\) (K)
- π :
-
Reduced pressure, P/PC
- ρ :
-
Density (kg m−3)
- σ :
-
Surface tension (N m−1)
- τ :
-
Time (h)
- 1.1:
-
Thermophysical properties at P0.1 = 0.1013 MPa
- C:
-
Property under critical conditions
- S:
-
Property under saturated conditions
- w:
-
Property at wall (heating surface) temperature
- calc:
-
Calculated value
- exp:
-
Experimental value
- ′:
-
Liquid phase
- ″:
-
Vapor phase
- CTAB:
-
Cetyltrimethylammonium bromide
- EDX:
-
Energy-dispersive X-ray analysis
- HTC:
-
Heat transfer coefficient
- IBC:
-
Internal boiling characteristics
- LSED:
-
Limited set of experimental data
- RMSE:
-
Root mean square error
- SEM:
-
Scanning electron microscopy
- SDBS:
-
Dodecylbenzenesulfonic acid sodium salt
- SDS:
-
Dodecyl sulfate sodium salt
- ST:
-
Spectral turbidity
- TEM:
-
Transmission electron microscopy
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Acknowledgements
This work was supported by Ministry of Education and Science of Ukraine (Project Number 0118U000237), the Foundation for Science and Technology (FCT), Portugal (Project Number UID/EEA/50009/2019) and EU COST Action CA15119 (NANOUPTAKE). Authors appreciation goes to María Echeverría for her help with TEM measurements.
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Khliyeva, O., Zhelezny, V., Lukianova, T. et al. A new approach for predicting the pool boiling heat transfer coefficient of refrigerant R141b and its mixtures with surfactant and nanoparticles using experimental data. J Therm Anal Calorim 142, 2327–2339 (2020). https://doi.org/10.1007/s10973-020-09479-0
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DOI: https://doi.org/10.1007/s10973-020-09479-0