Testing and evaluation of off-gas filters for bioreactors by a new bacterial aerosol challenge test method (TBAC).

A TNO bacterial aerosol challenge (TBAC) filter test rig was developed for direct assessment of the effectiveness of bioreactor off-gas filters as an alternative to routinely applied indirect wet integrity testing (IT). This TBAC test rig is based on bacterial aerosol challenging with Pseudomonas diminuta and dual monitoring by laser particle counting (LPC) and Andersen microbial sampling (AMS) of viable cells. The TBAC filter test rig is able to reproduce the various conditions encountered in fermentation processes. In experiments with several filters from one class, it was demonstrated that some filters were actually penetrated by up to 3,000 viable cells per test, despite their approval by commercially available IT test equipment. Repetitive filter use, prolonged use, and autoclaving of filters resulted in an increase in pressure drop over the filter but improved the performance of leaking/deviant filters due to building up of a filter cake (this phenomenon was identified by electron microscopy). The integrity tests used were found inadequate for accurate assessment of filter quality. Certification of filter lots by random tests of commercially available off-gas filters using sensitive direct methods such as those presented here might be advisable, as not all filters purchased were of appropriate quality.

Extractive purification of enzymes from animal tissue using aqueous two phase systems: pilot scale studies.

Pilot scale trials have been carried out to assess the feasibility of using PEG-salt aqueous phase systems for extraction and purification of enzymes from animal tissue on an industrial scale. Comminuted bovine liver was used as a starting material, and it was easy to separate a clear upper phase containing proteins of interest from a mixture containing 20% biomass, 15% PEG and 8% phosphate using a disc separator. Similar attempts with decanters were unsuccessful. Second-phase separation was simply accomplished by the addition of salt to the separated, clear upper layer and standing or allowing passage through a disc separator. The method was tested using continuous mixing on the GBF continuous mixing aqueous phase extraction plant, with and without computer control. Good separations were achieved. The enzyme superoxide dismutase was purified using this method yielding a 4-fold purification factor with respect to soluble protein and a recovery rate of 83%, with the enzyme in a clarified solution suitable for further processing by chromatographic methods. The general applicability of this method, its economics and its potential application in industry are discussed.

Inhibition of microbial cholesterol oxidases by dimethylmorpholines.

Cholesterol oxidase is a potentially important enzyme in steroid transformations, catalysing the conversion of 3-hydroxy-5-ene steroids to 3-keto-4-ene derivatives via a 3-keto-5-ene intermediate. Morpholine derivatives, especially fenpropimorph and tridemorph, were found to block selectively the isomerisation activity of cholesterol oxidases isolated from Nocardia erythropolis, Streptomyces sp., Pseudomonas testosteroni and Schizophyllum commune. These enzymes differ strongly in physical characteristics and catalytic behaviour. The effectiveness of the inhibitors varied with the cholesterol oxidase tested. Fenpropimorph was most effective with each of the 4 enzymes, 50 mg/l inhibiting about 50% of the enzyme activity. Inhibition was instantaneous and followed a reversible competitive mechanism in Streptomyces sp. and a reversible non-competitive mechanism in Nocardia erythropolis and Schizophyllum commune. An irreversible type of inhibition was observed for P. testosteroni cholesterol oxidase.

Kinetic aspects of the bioconversion of L-tyrosine into L-DOPA by cells of Mucuna pruriensL. Entrapped in different matrices.

Plant cells of Mucuna pruriens L. entrapped In calcium alginate, calcium pectinate, agarose, or gelatine were able to convert L-tyrosine to L-DOPA, which was released Into the medium. Michaelis-Menten kinetics could be applied on the entrapped cells, based on the measurement of initial rates of L-DOPA production. The calculated apparent affinity constants were comparable with the affinity constants obtained with enzyme preparations. Comparison of the apparent maximum rate of bioconversion of the entrapped cells and the maximum rate of bioconversion of a derived cell homogenate indicated that the systems were not operating optimally. Measurement of the effective diffusion coefficients of L-tyrosine pointed out that this substrate could diffuse freely into the matrices. From the initial rates of bioconversion and the effective diffusion coefficients, the observable modulus was calculated for each system. The obtained values confirmed that the diffusional supply rate of L-tyrosine was not the limiting factor. For oxygen, which was utilized for byconversion as well as for cell respiration, the calculated observable moduli was directed toward strong oxygen transfer limitations. The values found for the oxygen consumption indicated that the entrapped cells remained partly or totally viable in the four matrices tested. Based on the highest viability and the highest rates of bioconversion, it was concluded that alginate-entrapped cells of M. pruriens formed the most suitable biocatalytic system for the production of L-DOPA from L-tyrosinre.

Further kinetic characterization of alginate-entrapped cells of Mucuna pruriens L.

Alginate-entrapped cells of Mucuna pruriens L. hydroxylate L-tyrosine, tyramine, para-hydroxyphenylpropionic acid, and para-hydroxyphenylacetic acid to their corresponding catechols, which were released into the incubation medium. Michaëlis-Menten kinetics was applied for each bioconversion. The apparent affinity constants were comparable with the affinity constants obtained with a homogenate directly prepared from the cells used for entrapment and with a derived partly purified phenoloxidase. The values found for the apparent maximum rates of bioconversion of the entrapped cells were ca. 50% of the values of the maximum rates of bioconversion of the cell homogenate, indicating that the entrapped cell system was not operating optimally. The effective diffusivities of the substrates and products were measured with alginate-entrapped, inactivated cells. From the five inactivation methods tested, glutaric aldehyde treatment was chosen as the general procedure. Calculated effective diffusivities for the monophenols and catechols demonstrated that these compounds could diffuse freely into and out of the beads. For each bioconversion, the observable modulus was calculated from the initial rate of bioconversion and the effective diffusivity of the substrate. The resulting values indicated that the diffusional supply rate of the substrates was not the limiting factor, except for the conversion of tyramine for which a modulus higher than one was obtained. Analogously, the observable moduli were calculated for oxygen, which was utilized for bioconversion and cell respiration, and these values pointed towards strong oxygen limitation in all cases. The bioconversion rates of the entrapped cells increased with decreasing cell aggregate size. Therefore, it was concluded that direct cell-matrix contact determined the amount of phenoloxidase involved in the bioconversions. The bioconversion rate on a protein basis was constant with enhancement of the bead charge and thus, in spite of limitations, the mixing conditions as such were relatively optimal. In conclusion, the nonoptimal efficiency of the plant cell system studied was caused by oxygen limitation and a partial phenoloxidase participation, but not by mass transfer limitations for substrates and products with the exception of the conversion of tyramine into dopamine.