Heat transfer and pressure drop in flows of air-water mixtures have be
en investigated experimentally in an isoflux vertical annulus The supe
rficial liquid Reynolds number, as a reference parameter, varied from
4500 to 30000, at different values of gas-to-liquid superficial veloci
ty ratios zip to 20 and surface heat fluxes from 50 to 240 kW/m(2). En
hancement of the two-phase heat transfer coefficient is pronounced par
ticular ly at low liquid superficial velocities. The results are corre
lated and compared with some models of two-phase, two-component flows
for air-water mixtures within their range of validity. Satisfactory ag
reement is obtained from the trend of the experimental data.