Spin coating of two commercially used polymer solutions is studied bot
h theoretically and experimentally. Physical and theological character
ization of these solutions indicates that under the spinning condition
s currently used they behave as nonvolatile, viscoelastic fluids with
constant viscosity and elasticity. The corresponding Reynolds (Re) and
Deborah (De) numbers are up to order unity. The theoretical analysis
demonstrates and explains why, at very short times after the inception
of impulsive spinning, the velocity and stress fields in such fluids
develop in an oscillatory manner. The amplitude of these oscillations
increases with the ratio of the retardation parameter to the Deborah n
umber, whereas their damping rate gets smaller as De increases. Since
these oscillations dissipate very rapidly, and before substantial thin
ning of the film takes place, the thinning rate, velocity, and shear s
tress components do not deviate eventually from those of a Newtonian f
luid. Such a complete explanation of similar experimental findings has
not been offered before, The radial normal stress component does incr
ease considerably over its Newtonian value, and this explains certain
''experimental practices.'' Similar oscillatory development early on o
ccurs even at higher Re, as long as Re similar to De, but it is dissip
ated again, this time because of the abrupt thinning of the film. The
theoretical results are in good agreement with experimental measuremen
ts of ''dry film'' thickness and with dynamical measurements of ''wet
film'' thickness during spinning, which are reported herein for the fi
rst time. Care must be taken in reporting ''dry film'' thickness becau
se the commercial solutions under study retain part of the solvent aft
er ''soft baking'' over a hotplate. Complete solvent removal produces
dry films, but requires treatment in a vacuum oven, higher temperature
s, and longer heating times.