The chemical and gas phase equilibrium of the direct
synthesis
of dimethyl carbonate (DMC) from methanol (MeOH) and CO2 was modeled under mild conditions of temperature and pressure. Deviations
from ideality for the quaternary mixture (CO2 + MeOH +
DMC + H2O) were estimated using the γ – ϕ
thermodynamic approach. Binary interaction parameters (k
ij
) and UNIQUAC parameters (A
ij
) were extracted from VLE data reported
in the literature. The results show that MeOH conversion is enhanced
by increasing the pressure and reducing the temperature; however,
pressure and temperature are bounded by the dew point. Data of P, T, and vapor compositions obtained from
modeling chemical equilibrium were used to predict dew points of the
reacting mixture and to establish the region of T and P where the gas-phase reaction could be carried
out. To avoid condensation, an increase in pressure must be accompanied
by a temperature increase. Moreover, the larger the methanol concentration
in the feed mixture is, the higher is the required temperature.