A photoevaporative mass-transfer measurement technique has been used t
o determine the convective mass-transfer behavior of stationary and ro
tating cylinders which were immersed in a two-dimensional jet of air.
For a stationary cylinder, the circumferential distributions of the lo
cal mass-transfer rate were determined as a function of jet Reynolds n
umber (45000-176000) and ranges of other parameters of practical impor
tance (relative position of cylinder in jet (LID) and relative size of
cylinder and jet nozzle (d/D)). Circumferentially averaged values of
the mass-transfer coefficient were estimated by integration and the re
sults used to produce correlations for the mean Sherwood number. For a
rotating cylinder immersed in the slot jet, circumferentially average
d values of Sherwood number were directly determined for a range of co
nditions similar to those used in the study of the stationary cylinder
but with rotational speed as an additional variable. Predictions of t
he mean Sherwood number for cylinders drying in a slot jet have been m
ade using a CFD package and are presented in the form of correlations.