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D J Kirwan

Publications and source records attributed to D J Kirwan.

5 recordsLinked to original sources

Ceramic membrane microfilter as an immobilized enzyme reactor.

This study investigated the use of a ceramic microfilter as an immobilized enzyme reactor. In this type of reactor, the substrate solution permeates the ceramic membrane and reacts with an enzyme that has been immobilized within its porous interior. The objective of this study was to examine the effect of permeation rate on the observed kinetic parameters for the immobilized enzyme in order to assess possible mass transfer influences or shear effects. Kinetic parameters were found to be independent of flow rate for immobilized penicillinase and lactate dehydrogenase. Therefore, neither mass transfer nor shear effects were observed for enzymes immobilized within the ceramic membrane. Both the residence time and the conversion in the microfilter reactor could be controlled simply by regulating the transmembrane pressure drop. This study suggests that a ceramic microfilter reactor can be a desirable alternative to a packed bed of porous particles, especially when an immobilized enzyme has high activity and a low Michaelis constant.

Biotechnology↗

Effects of fluid shear on immobilized enzyme kinetics.

There have been a number of reports concerning the damaging effects of shear on globular proteins in solution. Some recent work has indicated, however, that globular proteins in solution are relatively stable, but may be inactivated at air-liquid interfaces during shearing. This study investigated the effects of fluid shear on immobilized enzyme activity. Immobilized enzyme reactors were built to operate with the enzyme immobilized at the boundary of a fluid flow field. Two different enzymes, penicillinase and lactate dehydrogenase, were covalently bound to the interior surface of nylon tubes. Fluid shear rate was changed by varying the flow rate of substrate (reactant) solution through the tube, and fluid shear stresses were increased by increasing the viscosity of the recirculating solution. There were no observed effects of fluid shear on immobilized penicillinase or lactate dehydrogenase activity at shear rates of up to 10,350 s-1 or at shear stresses of up to 73 Pa.

Animals↗

Nitrogenase activity of immobilized Azotobacter vinelandii.

As part of a program to investigate the use of biological nitrogen fixation for fertilizer ammonia production, an investigation into the immobilization of the aerobic, nitrogen-fixing bacterium, Azotobacter vinelandii was undertaken. Immobilization was acaccomplished by adsorption onto an anionic exchange cellulose (Cellex E) with loadings as high as 10'' cells/g resin. Immobilized cell preparations were tested under both batch and continuous-flow conditions. Nitrogenase activities as high as 4200 nmol/min g resin were observed as measured by the acetylene reduction assay. Immobilized cells retained their activity for as long as 117 hr in a continuous-flow reactor. Activity loss appeared to be related to the development of a variant strain.

Acetylene↗

Cell growth and monoclonal antibody production in the presence of antigen and serum.

The impact that the continuous presence in the fermentation broth of the cognate antigen has on the serum-supplemented hybridoma cell cultures was investigated. Both soluble and immobilized antigen at various concentrations was applied. The cell line (ATCC TIB191) was cultured in a serum-supplemented PFHM-II medium in T-flasks. Sepharose gel beads provided the immobilization matrix, and bovine gamma-globulin was the carrier protein upon which the antigen, picric acid, was conjugated. Produced antibody, after elution from the beads by displacement with free picric acid, was measured with an ELISA. Soluble antigen--carrier protein conjugates showed no effect on the cultures, but the immobilized antigen had a strong influence on them. Cell growth rate and total antibody production decreased as the amount of immobilized antigen increased from 16:10 (units are in (mol of Ag/mol of carrier):(mg of carrier/mL of beads) to 36:40. Most importantly, the specific antibody production rate switched from growth phase-independent behavior in the antigen-free cultures to growth phase-dependent behavior in the immobilized antigen cultures. Furthermore, during the early stationary phase of the cultures with immobilized antigen, the specific antibody production was 20-100% higher relative to the production rate in antigen-free cultures. This increased specific antibody production rate would be particularly useful in increasing the volumetric productivity of perfusion-type bioreactors for hybridoma cell cultures.

Animals↗