RESUMEN
The synthetic polymer industry is transitioning from the use of organic solvents to aqueous media in order to reduce environmental impact. However, with radical polymerization kinetics affected by hydrogen-bonding solvents, there is limited information regarding the use of water as a solvent for sparingly soluble monomers. Thus, in this paper, the radical polymerization of methyl acrylate (MA) and N-tert-butylacrylamide (t-BuAAm) is studied in water and ethanol (EtOH), as the copolymer product is of commercial interest. A series of semi-batch reactions are conducted under a range of operating conditions (i.e., reaction temperature, solvent-to-monomer ratio, and comonomer composition) to demonstrate that the copolymer can be successfully synthesized without significant drifts in product molar masses or composition. The experiments provide additional data to probe the influence of the solvent on the polymerization rate and copolymer properties, as the low monomer concentration maintained under starved-feed operation leads to a solvent-to-monomer ratio different from that in a batch system. A model that captures the influence of backbiting and solvent effects on rate, previously developed and tested against batch polymerizations, also provides an excellent description of semi-batch operation, validating the set of mechanisms and kinetic coefficients developed to represent the system.
RESUMEN
The optimal conditions for the production of virulent bacteriophages in bioreactors can vary greatly depending on the host-bacteriophage system used. We present a general method for the production of virulent bacteriophages in bioreactors that can be adapted to many host-bacteriophage systems and various operating conditions (reactor volume, medium composition, temperature, etc.). The procedures detail how to establish optimal initial infection conditions (infection load and initial multiplicity of infection (MOI)), prepare the host pre-culture and bioreactor, operate the bioreactor, and harvest the bacteriophage product. Batch operation is detailed but a short discussion addresses other modes of operation, namely two-stage continuous bioreactors and two-stage cycling bioreactors.