Vola
tiliza
tion ra
tes of nea
t liquids (benzene,
toluene,fluorobenzene, bromobenzene, e
thylbenzene,
m-xylene,
o-xylene,
o-dichlorobenzene,
and 1-me
thylnaph
thalene)
andof solu
tes (phenol,
m-cresol, benzene,
toluene, e
thylbenzene,
o-xylene,
and e
thylene dibromide) from dilu
te wa
tersolu
tions have been measured in
the labora
tory over awide range of air speeds
and wa
ter-s
tirring ra
tes. The overall
transfer coefficien
ts (
KL) for individual solu
tes areindependen
t of whe
ther
they are in single- or mul
ti-solu
tesolu
tions. The gas-film
transfer coefficien
ts (
kG) forsolu
tes in
the
two-film model, which have hi
ther
to beenes
tima
ted by ex
trapola
tion from reference coefficien
ts, cannow be de
termined direc
tly from
the vola
tiliza
tion ra
tesof nea
t liquids
through a new algori
thm. The associa
ted liquid-film
transfer coefficien
ts (
kL) can
then be ob
tained frommeasured
KL and kG values
and solu
te Henry law cons
tan
ts(
H). This approach provides a novel means for checking
the precision of any
kL and kG es
tima
tion me
thods for ul
tima
tepredic
tion of
KL. The improved
kG es
tima
tion enablesaccura
te
KL predic
tions for low-vola
tili
ty (i.e., low-
H) solu
teswhere
KL and kGH are essen
tially equal. In addi
tion,
thepredic
tion of
KL values for high-vola
tili
ty (i.e., high-
H) solu
tes,where
KL ![](/images/en<font color=)
ti
ties/cong.gif">
kL, is also improved by using appropria
tereference
kL values.