Gas exchange in steady state foams was measured. Foams were beaten in
a thermostated cylindrical vessel with a vertical rotating cage and ar
gon or hydrogen gas of constant flow rate was led into the bottom of t
he vessel. After reaching steady state, the gas stream was switched to
nitrogen. The vessel was tightly covered and the effluent gas was mon
itored by a katharometric cell. The break-through curve of nitrogen wa
s registrated. A mathematical model was constructed for the simulation
of the break-through curves. In the model, the rate of gas incorporat
ion, I-ht the rate of by-passing through vertical channels, and the ve
rtical mixing of the foam were taken into consideration. The value of
I-h has been known from the parameters of the fitted break-through cur
ve. The rate of surface formation was calculated as the, product of I-
h and a(h). The results were compared to the rate of surface collapse
in stationary foams.