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Transition boiling heat transfer in a vertical round tube

Technical Report ·
DOI:https://doi.org/10.2172/6494140· OSTI ID:6494140
Transition boiling heat transfer coefficients have been obtained for water at pressures of 25 to 75 psia and mass velocities from 14,000 to 140,000 lbs/hr ft/sup 2/. The water flowed inside a 1/2 in O.D. tube and was heated by hot mercury flowing in an annulus around the tube. Thermocouple pairs placed on the outside of the central tube and outer pipe at several axial elevations allowed the rate of heat transfer to be determined. The data agreed reasonably with the correlation previously proposed. However, the observed heat transfer coefficients show less of a decrease with increasing temperature than was seen in previous tests in which the water flowed in an annulus.
Research Organization:
Cincinnati Univ., OH (USA). Dept. of Chemical and Nuclear Engineering
OSTI ID:
6494140
Report Number(s):
EPRI-NP-895
Country of Publication:
United States
Language:
English