Experimental Study of Horizontal Flow Boiling Heat Transfer Coefficient and Pressure Drop of R134a from Subcooled Liquid Region to Superheated Vapor Region
Abstract
:1. Introduction
2. Experimental Set Up
2.1. Measurement
2.2. Fluid Temperature
2.3. Heat Flux
2.4. Vapor Quality
2.5. Accuracy of Measurement
2.6. Data Reduction
2.7. Frictional Pressure Drop
2.8. Experimental Validation
2.9. Experimental Method
3. Results and Discussion
3.1. Subcooled Region
3.2. Two-Phase Region (Saturated Region)
3.3. Dry-Out Incipience and CHF
3.4. Superheated Region
Visualization of Flow Pattern
3.5. Temperature Profile
4. Pressure Drop
5. Conclusions
- At the low saturation pressure and heat flux conditions studied, a maximum peak of the heat transfer coefficient near the vapor quality of zero (0) was observed. This peak was sensitive to heat flux and insensitive to mass flux.
- After the local maximum peak of the heat transfer coefficient reached near zero vapor quality, heat transfer coefficient deterioration is observed until a local minimum is reached. The decrease in heat transfer coefficient to a local minimum is observed at a low vapor quality region below 0.1 (i.e., x < 0.1).
- Heat flux had a considerable impact on the heat transfer coefficient in the low-vapor-quality region. However, this influence was reduced as vapor quality increased. The influence of mass flux in the low vapor quality region was mild, except at low heat fluxes. In the high vapor quality region, the effect of mass flux on the heat transfer coefficient was highly pronounced. Generally, in the low vapor quality region, nucleate boiling heat transfer was the dominant mechanism controlling the heat transfer coefficient, whereas in the high vapor quality region, convective heat transfer was the dominant mechanism.
- The flow patterns observed were recorded with a high-speed camera to help analyze the results. The main flow patterns observed were slug, intermittent in the low-quality region, and annular and dry-out to mist in the high-quality region.
- Pressure drop varied as a function of vapor quality and mass flux in the two-phase region and superheated vapor region. There was no significant effect of heat flux on pressure drop.
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
Nomenclature
D | Channel diameter (m) |
h | Heat transfer coefficient (W/(m2 K)) |
G | Mass flux (kg/(m2s)) |
k | Thermal conductivity of liquid (W/(m K)) |
Nu | Nusselt number (hD/k) |
Pr | Prandtl number |
PrL | Liquid phase Prandtl number |
PrV | Vapor phase Prandtl number |
ReL | Liquid Reynolds number |
Tsub | Inlet subcooling (K) |
ReV | Vapor Reynolds number |
Re2φ | Two-phase Reynolds |
x | Vapor quality |
q″ | Heat Flux (Wm−2) |
hlv | Latent heat of vaporization (J/(kg K) |
hl | Specific enthalpy of liquid (J/(kg K)) |
g | Acceleration due to gravity (ms−2) |
A | Cross section area (m2) |
Tw,i | Inner wall temperature (K) |
Tf | Fluid temperature (K) |
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Experimental Condition | Mass Flux (G (kg/(m2s)) | Heat Flux (q″ (kW/m2)) | Saturation Pressure (P (kPa)) |
---|---|---|---|
1 | 200 | 4.6 | 460 |
2 | 200 | 8.5 | 460 |
3 | 300 | 4.6 | 460 |
4 | 300 | 8.5 | 460 |
Properties | Saturation Pressure = 460 kPa |
---|---|
Saturation Pressure | 13.150 °C |
Liquid Density | 1250.0 kg/m3 |
Vapor Density | 22.397 kg/m3 |
Liquid Enthalpy | 217.92 KJ/kg |
Vapor Enthalpy | 406.06 KJ/kg |
Liquid Viscosity | 2.258 × 10−4 Pa·s |
Vapor Viscosity | 1.1219 × 10−5 Pa·s |
Liquid Conductivity | 86.247 mW/m·K |
Vapor Conductivity | 12.690 mW/m·K |
Surface Tension | 9.6121 mN/m |
Variable | Symbol | Accuracy | Information |
---|---|---|---|
Mass flux | G | 0.2 % of the reading | Given by the supplier |
Pressure drop | ΔP | 0.075 % full scale (fs = 50 kPa) | Given by the supplier |
Absolute pressure | P | 0.04 % full scale (fs = 25 bar) | Given by the supplier |
Temperature | T | 0.1 K | Inhouse calibration |
Heat flux | q″ | 3% of the reading | Inhouse calibration |
Parameter | Symbol | Error |
---|---|---|
Mass flux | G | ±10 kg/m2s |
Inlet pressure | Pi | ±10 kPa |
Inlet temperature | Ti | ±0.2 °C |
Heat flux (all 5 zones) | q″ | ±<40 W |
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Bediako, E.G.; Dančová, P.; Vít, T. Experimental Study of Horizontal Flow Boiling Heat Transfer Coefficient and Pressure Drop of R134a from Subcooled Liquid Region to Superheated Vapor Region. Energies 2022, 15, 681. https://doi.org/10.3390/en15030681
Bediako EG, Dančová P, Vít T. Experimental Study of Horizontal Flow Boiling Heat Transfer Coefficient and Pressure Drop of R134a from Subcooled Liquid Region to Superheated Vapor Region. Energies. 2022; 15(3):681. https://doi.org/10.3390/en15030681
Chicago/Turabian StyleBediako, Ernest Gyan, Petra Dančová, and Tomáš Vít. 2022. "Experimental Study of Horizontal Flow Boiling Heat Transfer Coefficient and Pressure Drop of R134a from Subcooled Liquid Region to Superheated Vapor Region" Energies 15, no. 3: 681. https://doi.org/10.3390/en15030681