Potential of Pervaporation-Based Dehydration Processes
as an Equilibrium-Limited Reactions Enhancer: Proof-of-Concept and
Process Scale-up for an Acrylic Ester
posted on 2021-11-09, 17:10authored byDânia S. M. Constantino, Alírio E. Rodrigues, Rui P. V. Faria
Chemicals derived from equilibrium-limited
reactions represent
a huge challenge mainly from the process sustainability point of view.
Usually, high temperatures are required to reach reasonable kinetic
rates and interesting yields. Apart from a high energy demand and
operating costs, some of those compounds are temperature-sensitive,
such as butyl acrylate, for instance, which polymerizes above 100
°C. Therefore, other alternatives have been investigated to attain
competitive yields from the industrial point of view, reducing the
energy required through process intensification strategies. This work
focuses on a strategy for combining an effective separation process
with a reaction. Pervaporation technology was coupled with a fixed-bed
reactor for the production of butyl acrylate while water is continuously
removed from the reaction medium enabling a shift of the reaction
equilibrium. This approach benefits complex reactions with limited
operating temperature ranges, either because of product yield constraints
or parallel reactions, such as the polymerization of acrylic acid
and butyl acrylate. The benefits of membrane separation for this kind
of reaction were addressed in this work, where the proof-of-concept
was shown comparing the process operating with and without a membrane
module. A significant difference in butyl acrylate molar composition
was observed, which increased 16%, while the water molar composition
decreased about 40%. Moreover, the mathematical model was validated
successfully, and different operating parameters were evaluated by
process simulation. All the results provided are considered valuable
for the design of pervaporation-based process intensification strategies
at a large scale working in continuous mode operation. Finally, a
simple strategy comprising a coupled reaction–separation configuration
at the industrial scale is proposed and assessed for the continuous
manufacturing of butyl acrylate.