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This paper presents experimental results for the heat transfer coefficient during flow boiling of refrigerants R134a, R245fa and R600a inside small diameter tubes. The experimental database comprises over 2000 data points covering tube diameters from 0.38 to 2.6 mm, mass velocities from 49 to 2200 kg/m2s, and heat fluxes up to 185 kW/m2. The effects of experimental parameters like mass velocity, tube diameter, heat flux, refrigerant type and saturation temperature on the heat transfer coefficient and dryout

Author

hamed hatami

Language

EN