The heat transfer rate in gas–liquid bubble columns is reported to be generally 100 times greater than in single phase flow (Deckwer, 1980) This rate is
The model assumptions of Luke and Gorenflo for the heat transfer near growing and departing bubbles, which were applied in the calculations, have been slightly
is found that the temperature of bubble initiation on a given surface is heat transfer near the knee of the boiling curve using only an experi-
heat transfer resulting from Marangoni convection around a bubble situated on a heated wall was performed by Larkin [16] Larkin numerically simulated the
Possibly the first study aimed to quantify the rates of heat transfer resulting from Marangoni convection around a bubble situated on a heated wall was performed