Methyl methacrylate is an essential chemical used as raw material
for the production of other methacrylates and poly-methyl methacrylate.
There are various chemistry routes, available or not on the industrial
scale, to produce methyl methacrylate. These routes use the same or
different raw materials and present common chemistry and processing
steps. Many of these routes though, have as a final step the esterification
of methacrylic acid with methanol to obtain methyl methacrylate. However,
there is no complete process described in the literature for this
final esterification step. This paper is the first to propose a solid-based
catalytic process for methyl methacrylate production starting from
methyl methacrylate and methanol, in a continuous reaction–separation–recycle
system. In this specific case, this system is more suitable than reactive
distillation due to the unfavorable ranking of boiling points and
also due to the presence of several potentially hindering azeotropes.
This work also provides an original framework for simulation of other
methyl methacrylate processes, by deriving detailed equilibrium and
kinetic parameters based on literature experimental data. Rigorous
process simulations are carried out in Aspen Plus and Aspen Plus Dynamics
for the design and control of the new process. The flowsheet consists
mainly of a fixed-bed tubular reactor followed by a sequence of three
distillation columns coupled with a decanter. The results show that
the process is technically feasible, cost-effective in terms of total
annualized costs, and with excellent sustainability metrics, requiring
only 2.05 MJ/kg of methyl methacrylate produced.