A set of experiments has been performed to analyse gas-phase distribution i
n horizontal bubble flow. The experimental data have been obtained by means
of conductance probes and include measurements of the local void fraction
and the bubble diameter and velocity. Present observations show large varia
tions of the local void fraction and the bubble size moving from the top to
the bottom of the pipe, with local maxima located close to the upper pipe
wall. Measurements also show that, at the boundary of the dispersed bubble
flow regime, the bubble size, and therefore the surface available for heat
and mass transfer, changes abruptly for small variations of the liquid or g
as flowrate. This change allows the transition between the dispersed and th
e elongated bubble regimes to be identified with good precision. Present da
ta make it possible to develop a new correlation for the maximum bubble siz
e in dispersed bubble flow. (C) 1999 Elsevier Science Ltd. All rights reser
ved.