The results of the experimental studies of local heat process for a gasliquid system in the region of the cylindrical wall of an agitated vessel equipped with the system of CD 6RT impellers are presented. A lower CD 6 impeller (Smith turbine) and upper RT impeller (Rushton turbine) were located on the common shaft in a baffled agitated vessel of inner diameter equal to 0.3 m. Liquid height in the agitated vessel was equal to 0.6 m. Newtonian liquids of different physical properties were used as a continuous phase. Air was dispersed in the liquid. Local heat transfer coefficients were measured using both thermal and electrochemical methods. In total, 2280 experimental points were obtained. Distributions of the heat transfer coefficients were described by means of eqs 1217 and 1823 as a function of the Re and Pr numbers, dimensionless axial coordinate z/H, and modified Fr-g number, separately, for turbulent and transitional ranges of the fluid flow in the agitated vessel. Equations 1217 and 1823, concerning both coalescing and noncoalescing gasliquid systems, have no equivalent in the open literature.