This paper aims at intensifying the
synthesis process of solketal
by the reactive dividing wall column (RDWC) through experiments and
simulation optimization and proposes a high-efficiency production
process of solketal. A lab-scale RDWC was set up to verify the feasibility
of synthesizing solketal in the RDWC. The effects of different operating
parameters, such as reflux ratio, liquid split ratio, molar ratio
of acetone to glycerol, feeding method, and the mass flow rate of
side stream, on the experimental process have also been demonstrated
and analyzed. Furthermore, an equilibrium-stage model developed by
Aspen Plus and verified through comparison with experiments was used
for the following simulation to optimize and analyze the solketal
synthesis process. The response surface methodology (RSM) was employed
to optimize the multiobjective problem in RDWC. As a result, a novel
competitive solketal synthesis process with an upper partition position
RDWC was put forward, which could obtain 99.78% conversion and 99.22
wt % solketal product purity at a 2:1 molar ratio of acetone to glycerol
and had a lower energy consumption per unit mass product of 2509.2
J·g–1 compared with other processes. The achievements
of this research provide a new way to produce solketal and a significant
guideline for the industrial applications of solketal synthesis in
the reactive dividing wall column.