Scraped surface heat exchangers (SSHE) are prevalent in the food industry t
o heat/cool viscous fluids and to provide enhanced mixing. This work focuse
d on developing and verifying a theoretical model to characterize the flow
patterns in two-dimensional angular flow in an SSHE geometry under isotherm
al conditions. Experimentally, the model was verified by a noninvasive magn
etic resonance imaging (MRT) technique. Good agreement was achieved between
the theoretical model and experimental data for a polyalkylene glycol, whi
ch behaved as a Newtonian fluid (n = 1), and a 1% CMC solution, a power law
fluid with n = 0.77. However, the experimental flow profile tomato puree w
as characterized by apparent wall slip. The best fit, with respect to the p
ower law model, was a flow behavior index of 0.11. This study provides the
framework to quantify the effects of heat transfer on flow profiles in this
geometry and the effectiveness of mixing.