It is envisaged that the future refineries
will be reconfiguring
for the direct conversion of crude oil to chemicals to improve their
profitability. In this direction, the toluene methylation process
offers a promising route for the production of high-value p-xylene from low-cost feedstocks such as toluene and methanol.
There is a growing commercial interest in the toluene methylation
process, because it can theoretically produce double the amounts of p-xylene with high selectivities, when compared with the
other existing processes (such as disproportionation and transalkylation),
and it can be the next-generation method of producing p-xylene. Past and current research approaches were mainly focused
on improving the catalyst activity (high toluene conversion and para-selectivity) by introducing several modifying agents.
However, still the major challenge of this process lies in the development
of an efficient catalyst without compromising on the methylation activity
and para-selectivity. In addition, catalyst deactivation
is another major issue that is mainly due to the coking precursors
derived from methanol conversion. To address these issues, a good
understanding of the mass transfer plays a vital role in the catalyst
design, as well as process design and optimization strategies. This
review summarizes the fundamental aspects of possible reaction mechanisms
that occur in the process, useful reaction kinetics data for the process
optimization studies and scaleup, with emphasis on recent developments
in the catalyst design, deactivation mechanism, and process development
strategies. A future perspective is also provided related to the catalyst
design and process design strategies for addressing the gaps in this
field.