An electrochemical technique was used to measure local and instantaneous wa
ll shea rates in a scraped surface heat exchanger (SSHE). The inner cylinde
r; equipped with two blades symmetrically opposed, was driven by a stepping
motor and the outer cylinder was fixed. Highly viscous Newtonian fluids (E
mkarox HV45 solutions) and non-Newtonian model fluids (aqueous solutions of
guar and CMC) were used. The reliability of the electrochemical technique
was validated for these fluids in an annular space (SSHE without blades). T
he evolution of the limiting diffusion current was given by the probes in a
scraping situation. In the general case of scraping, the flow was unsteady
, and very fast large fluctuations of the limiting diffusion current were m
easured The shear rate at the wall of the stator of the SSHE appeared fully
controlled by the rotation of the blades. Then electrodiffusion measuremen
ts were interpreted using three different wall shear rate calculating proce
dures. Wall shear rate in SSHE appeared ten to 100 times more important tha
n in annulus, and the lowest values of the clearance between the edge of th
e blades and the stator was about 50 x 10(-6) m.