A simple
and practical process was developed for the efficient
separation of diastereomeric syn- and anti-2,4-pentanediol by selective acetalization of a diastereomeric mixture
of the 2,4-pentanediols and selective hydrolysis of the corresponding
acetals. The process relies upon the reaction rate differences of syn-2,4-pentanediol (syn-diol) and anti 2,4-pentanediol (anti-diol) in acetalization
and of the corresponding acetals in hydrolysis: the syn-diol reacts faster to form a more stable acetal than the anti-diol, which in turn is more susceptible to hydrolysis
by Brønsted acid. Acetalization of a 2,4-pentanediol diastereomeric
mixture (syn/anti = 45:55) with
acetophenone (0.95 equiv relative to syn-diol) leads
to the formation of a syn-enriched acetal mixture
with a syn/anti diastereomeric ratio
(dr
s/a
) of 6:1, leaving
an anti-enriched diol mixture (dr
s/a
= 1:7). Subsequent kinetic resolution via
selective hydrolysis of the minor anti-acetal with
a catalytic amount of 1.0 N HCl at ambient temperature affords the
pure syn-acetal (dr
s/a
> 99:1) in the organic phase and the anti-enriched 2,4-pentanediols (dr
s/a
= 1:6) in the aqueous phase, which are
conveniently separated
by a phase cut. Hydrolysis of the syn-acetal is facile
in alcohol solvents at elevated temperatures (60–80 °C),
yielding the pure syn-diol. A second acetalization
of the anti-enriched 2,4-pentanediols leads to the
pure anti-2,4-pentanediol. This separation gives
the syn-diol in 75–79% yield with dr
s/a
> 99:1 and the anti-diol in 79–85% yield with dr
a/s
> 98:2. Additionally, the acetophenone used for
the acetalization can be recovered in 88–92% yield, and therefore,
the overall process is high-yielding, atom-economical, and potentially
recyclable.