Membrane technology allows the separation of different species from a liquid or gas stream.
Membranes are semi-permeable materials: they selectively allow certain species to pass, while retaining others. For separation to occur, a driving force must be applied to membranes to cause one species to permeate the membrane. This driving force is often a pressure, heat, or concentration gradient, depending on the membrane process that is implemented. Separation processes utilizing membrane technology are often preferred due to their energy efficiency, modularity, and small process footprint, compared to conventional separation processes such as distillation and extraction.
The structure and performance of membranes can vary significantly for different processes. In liquid separations, membranes are primarily categorized according to the size of the components they can separate from the feed stream. For pressure-driven separation processes of liquid streams, the following membrane categories exist:
Reverse osmosis (RO) derives its name from the reversal of natural osmosis by the application of pressure. In RO processes, a pressure gradient is applied to desalinate saline water streams by allowing the selective permeation of water and the rejection of salts by a semipermeable membrane.
RO membrane structure is typically asymmetric or a thin film composite (TFC), where a thin, dense separation layer sits on top of a more porous support layer. State-of-the-art RO membranes are TFCs with dense polyamide separation layers (50 – 200 nm thick, ~5 Å free volume element size) with a polysulfone support layer (100 mm thick, 10 nm pore size). The rejection of solutes is primarily dominated by size exclusion and dielectric exclusion. These mechanisms produce a permeability-selectivity trade-off, where water permeability decreases when salt rejection increases, and vice versa. Maximizing permeability and selectivity are desired, thus many membrane scientists seek to push the limits of this tradeoff.
Organic solvent nanofiltration (OSN), also called solvent-resistant nanofiltration (SRNF), has emerged as a promising technology for the removal of impurities, recovery of solutes, and the regeneration of solvents in various industries, such as the pharmaceutical and the (petro)chemical industries. It is rapidly gaining importance as it contributes to process intensification and to a circular economy. Indeed, it is a versatile, energy-, waste-, and cost-efficient separation technique, with the potential to compete with or complement established separation processes, such as distillation or extraction. As OSN/SRNF membranes operate under harsh conditions, i.e., under pressure and in organic media (e.g., alcohols, toluene, DMF), the challenge is to produce materials with high selectivity, high flux, and long-term stability. In addition, knowledge gaps exist on the fundamental interactions between the solute, the solvent, and the membrane. Unawareness of the complex and interconnected behavior and characteristics of these three entities impedes successful prediction and accurate interpretation of OSN/SRNF processes.