Crystallization
faces great challenges from the point of view of
technology readiness, process economics, and energy consumption. Membranes
are capable of controlling both energy and mass transfer, and they
can lead to major improvements if integrated into antisolvent crystallization
processes, for example, limiting unfavorable kinetics and thermodynamics
that are responsible for undesired crystal size and shape. In this
work, membrane-assisted antisolvent crystallization (MAAC) was used
to crystallize the amino acid l-serine. Two commercial membranes
made of polyvinylidene fluoride and polypropylene with water contact
angles of 130° and 150°, respectively, allowed a controlled
antisolvent crystallization. These membranes controlled the transmembrane
mass transfer of antisolvent (ethanol) under different feed and antisolvent
velocities at ambient conditions. In all cases, a narrow crystal size
distribution of l-serine was obtained reflected in a coefficient
of variation (CV) of 31–37%, compared with batch antisolvent
crystallization or drop-by-drop crystallization where the CV was 63
and 54%, respectively. Thanks to the measurement of l-serine
and ethanol concentration along the operating time, the mass transfer
coefficient of MAAC was evaluated. Increasing the antisolvent or the
crystallizing solution velocity showed that a too high value of one
or the other could result in wetting or system blockage (inside the
membrane contactor, module, or tubing). This study explains the transmembrane
mass transfer in MAAC and the resulting crystal properties.