Non-Newtonian laminar boundary-layer heat transfer in stirred tanks

A laminar boundary-layer heat transfer in a jacketed, stirred tank with non-Newtonian fluids has been experimentally and theoretically examined. Heat transfer rates from jacket to process liquid through the stirred tank wall were measured for different large-scale impeller designs and rheological properties. On the basis of the laminar boundary-layer theory, we developed a theoretical correlation for non-Newtonian laminar tank-side film heat transfer coefficients in stirred tanks. The correlation was derived using von Karman's integral technique. Satisfactory agreement between the predictions of the proposed correlation and the present experimental data for viscous Newtonian and non-Newtonian laminar heat transfer in stirred tanks was obtained.