Heat transfer with steam condensation under moderate pressure on the s
urface of a horizontal tube immersed in a bubbling layer was experimen
tally investigated. A copper test section 16 mm in outer diameter and
400 mm in length was placed in a bubbling column 455 mm in diameter. E
xperiments were made under pressures of 0.14-0.8 MPa, with void fracti
on 0.04-0.23, vapor superficial velocities 0.05-0.42 m/s, liquid-wall
temperature differences 47-105 K, and heat flux densities 0.12-0.8 MW/
m2. The heat transfer process in the bubbling layer is shown to be of
a high intensity: with moderate values of steam content, heat transfer
coefficients reach 12-14 kW/(m2 . K). Data obtained showed that the k
nown correlations do not consider the influence of pressure on heat tr
ansfer. For the first time, data on radial steam content distribution
under pressures higher than atmospheric were obtained by an electropro
be method. A table of experimental data is presented.