22
Chemical Technology •May 2016
P
roviding adequate devolatilising facilities in-
volves both knowledge of equilibrium and
mass transfer limits. This study will appear in
three sections over the next few months, as follows:
Section 1 — In the first part I will discuss the theory and
show how the equilibrium and mass transfer limitations are
combined to estimate the required size of the devolatilisation
equipment. While this may sound too theoretical for the prac-
tising process engineer, the approach has been simplified
as much as possible while still being theoretically correct.
Section 2 — Here, I will discuss the determination of
equilibrium and how it may be calculated or determined
experimentally. The emphasis is on calculating since this is
the situation that many practising engineers find they must
handle, ie, laboratory facilities are not available to develop
actual data.
Section 3 — This part covers the development of mass
transfer coefficients from a pragmatic paradigm. In addition,
it describes a spreadsheet that is helpful in performing the
numerical integration.
When one is faced with a problem (either design or oper-
ating) that is associated with a volatiles removal operation,
the engineer is often tempted to use one of two incorrect ap-
proaches. He/she will assume the boiling point of the solvent
and the temperature of the solid are the primary variables
that determine whether the solid is sufficiently devolatised.
That is, no drying occurs unless the temperature of the solid
is above the boiling point of the volatile or that as long as
the solid is at a temperature above the boiling point of the
volatile, there will be no volatile remaining in the solid.
Both of these are wrong when considering either equi-
librium or mass transfer. A second approach is to recognise
Volatiles removal from solids
– An introduction to
devolatising
by Joe Bonem, Polymers and Process Engineering Consultant
Devolatilisation is a mandatory step in the
manufacturing of many commercial solids
ranging from pharmaceutical products to
waste streams. Excessive levels of residual
solvents, monomers or other volatiles can
create fires or explosions in subsequent
processing or transportation steps, as well
as discontinuities in product appearance.
The residual solvents or monomers may also
be odoriferous at very low concentrations,
creating end user concerns.




