Downstream
processing in the biorefinery is often faced with multicomponent
process streams containing carboxylic acids and alcohols. Isolation
of carboxylic acids may be simplified by direct esterification with
the alcohol present in the process stream. However, uncatalyzed esterification
is generally slow at moderate temperature. In multicomponent mixtures,
though, stronger carboxylic acids act as catalysts for the esterification
of weaker carboxylic acids. Single-acid esterification of formic acid,
acetic acid, and propionic acid with methanol were investigated, and
a kinetic model was developed considering the intramolecular catalytic
effect through acid dissociation. With the kinetic constants derived
from single-acid esterification, ester formation in multi-acid esterification
was predicted and verified experimentally with a maximum sum of mean
square error of 8.70 × 10–4. In multi-acid
esterification, the catalytic influence of formic acid on acetic acid
and propionic acid esterification was shown. Due to higher equilibrium
constants transesterification of methyl formate to methyl acetate
and methyl propionate, respectively, is observed and predicted by
the model.