A new model based on the quasi-stationary approximation is developed f
or removal of gas bubbles from glassmelts due to buoyant rise of bubbl
es. The growth and rising of multicomponent gas bubbles in glassmelts
are examined from the view point of interfacial mass transfer. It is s
hown that the models for rising bubbles in glassmelts available in the
literature are based on the quasi-steady approximation which is not v
ery reasonable. The growth of a gas bubble initially consisting of nit
rogen only is studied in a glassmelt whose diffusing gases are oxygen,
water, carbon dioxide, sulfide and nitrogen. The proposed model based
on the unsteady-state mass transfer (the quasi-stationary approximati
on) is compared with the model based on the steady-state mass transfer
(the quasisteady approximation). The former, which provides more rati
onal and better descriptions of bubble behavior in refining processes
compared with the latter, predicts rather shorter refining times than
the latter.