In this work, the separation of a
mixture of dimethyl carbonate
(DMC), formaldehyde, and water is studied. In our process, formaldehyde
is first extracted using water as the entrainer, and then the azeotrope
of DMC–water is separated by extractive distillation with ethylene
glycol. To verify the feasibility of the process, the liquid–liquid
equilibrium (LLE) data of the DMC–formaldehyde–water
system was measured and the vapor–liquid equilibrium (VLE)
data of the DMC–ethylene glycol system was also measured at
101.3 kPa. Moreover, the reliability of experimental tie-line data
was checked with the Bachman, Hand, and Othmer–Tobias equations,
and the thermodynamic consistency of the measured VLE data was verified
by the Van Ness test and infinite dilution test. Finally, all the
measured values were correlated with the nonrandom two-liquid (NRTL)
model and universal quasi-chemical (UNIQUAC) model, and the binary
interaction parameters were regressed.