The
autocatalytic hydrolysis kinetics of dimethyl oxalate (DMO)
was investigated in an isothermal batch reactor at 328.15–358.15
K. It was observed that DMO hydrolysis involved two reactions in series,
with monomethyl oxalate (MMO) as an intermediate product. The results
showed that water dominates the initial hydrolysis rate of DMO. In
later stages, oxalic acid plays a major role in catalyzing DMO hydrolysis
and MMO further hydrolysis. Based on these observations, a mechanism
involving the ionization of water and oxalic acid was developed that
assumes nucleophilic substitution to be the rate-determining step.
Concentration-based rate equations were further deduced including
the contribution of water startup and the catalytic action of oxalic
acid. In addition, the kinetic and equilibrium parameters were estimated
from the experimental data through regression analysis.