Gas-liquid bubbly flow was investigated in vertical pipes for differen
t flow conditions: fully developed turbulent downward flow in a 42.3 m
m diameter pipe and upward flow in a 14.8 mm diameter pipe with liquid
of elevated viscosity. Wall shear stress, local void fraction, and li
quid velocity profiles, shear stress, and velocity fluctuations were m
easured using an electrodiffusional method. Results obtained demonstra
te the existence of ''universal'' near-wall velocity distribution in a
downward bubbly flow. The reduction of turbulent fluctuations is obse
rved in downward flow as compared to a single-phase turbulent flow. Th
e development of bubble-induced liquid velocity fluctuations in a ''la
minar'' bubbly flow was studied.