W. J. J. Van Den Tweel

Kinetic aspects of glucose oxidation by Gluconobacter oxydans cells immobilized in calcium alginate

SummaryGluconobacter oxydans subspecies suboxydans (ATCC 621 H), when growing at high glucose concentrations, oxidizes this substrate incompletely and gluconic acid accumulates in the medium in almost stoichiometric amounts. Such cells were harvested and entrapped in various alginate gels. The preparation with the highest retention of glucose oxidizing activity was used in further studies with the aim of developing an efficient process for continuous gluconic acid production.The retention of activity increases (up to 95%) as the alginate concentration in the gel decreases or the cell/alginate weight ratio is enhanced. In the latter case, however, transport of oxygen to and inside the biocatalyst beads rapidly becomes rate-limiting and thus lowers the efficiency of the biocatalyst. Similarly, the efficiency decreases as the size of the biocatalyst beads increases. In no case rate-limitation by transport of glucose was found. Thus, biocatalyst activity per unit volume of support, diameter of the biocatalyst beads, and aeration efficiency are important parameters for reactor design.

Ochrobactrum anthropi NCIMB 40321 : a new biocatalyst with broad-spectrum L-specific amidase activity

Of 125 microorganisms that were able to use α-hydroxy acid amides as sole nitrogen source, Ochrobactrum anthropi NCIMB 40321 was selected for its ability to hydrolyse racemic amides l-selectively. The substrate specificity of whole O. anthropi cells is remarkably wide and ranges from α-H-α-amino-, α-alkyl-α-amino, N-hydroxy-α-amino acid amides to α-hydroxy-acid amides. After 50% conversion, both the l-acids formed and the remaining d-amides were present in >99% enantiomeric excess, and ammonia accumulated in stoichiometric amounts. Using mandelic acid amide as a model substrate, the hydrolysis was optimized. Optimal rates were observed at pH 8.5 at 50°C. At higher temperatures the initial rate was even higher; however, fairly rapid inactivation occurred.

Permeabilization and lysis of Pseudomonas pseudoalcaligenes cells by Triton X-100 for efficient production of d-malate

Pseudomonas pseudoalcaligenes can only form d-malate from maleate after incubation of the cells with a solvent or a detergent. The effect of the detergent Triton X-100 on d-malate production was studied in more detail. The longer the cells were incubated with Triton X-100, the higher was the d-malate production activity, until the maximal malease activity was reached. Incubation of P. pseudoalcaligenes cells with Triton X-100 also resulted in an increase in the protein concentration of the supernatant, indicating that cell lysis had occurred. The rate at which the d-malate production activity increased was dependent on the Triton X-100 concentration and on the cell density. Also the rate at which lysis occurred depended on the Triton X-100 concentration.

Production of 1-kestose with intact mycelium of Aspergillus phoenicis containing sucrose-1F-fructosyltransferase

SummaryFavourable reaction conditions for the enzymatic production of 1-kestose by sucrose-1F-fructosyltransferase, SFT (EC 2.4.1.99) from Aspergillus phoenicis CBS 294.80 mycelium were established. The intracellular enzyme SFT works best at 60°C, exhibits a relatively high thermostability and possesses an alkaline pH optimum. An invertase also present in the mycelium of A. phoenicis possesses an acidic pH optimum. Consequently, around pH 8.0 sucrose is converted mainly to 1-kestose and nystose while fructose is only formed in relatively small amounts. Under optimal conditions (55° C, pH 8.0 and an initial sucrose concentration of 750 g 1-1) a yield of about 300 g 1-kestose per 1.01 reaction mixture could be achieved after 8 h.

Chemo-enzymatic synthesis of amino acids and derivatives

A short overview is given of new developments in the chemo-enzymatic synthesis of amino acids. Amino acid resolution procedures based on stereoselective enzymatic hydrolysis of amino acid amides have been developed. Two enzymes, an aminopeptidase from Pseudomonas putida and an amidase from Hycobacterium neoaurum have been purified to homogeneity. In addition, methods for the stereoselective synthesis of a-alkyl-substituted hydroxy acids are given.

Catabolism of DL-a-phenylhydracrylic-, phenylacetic- and 3- and 4-hydroxyphenylacetic acid via homogentisic acid in a Flavobacterium sp.

A degradation pathway for dl-α-phenylhydracrylic, phenylacetic, 3- and 4-hydroxyphenylacetic acid by a Flavobacterium is presented. Experiments with washed cells and enzyme studies revealed that dl-α-phenylhydracrylic acid in an initial reaction was oxidatively decarboxylated to phenylacetaldehyde. Whole cells oxidized both stereoisomers of phenylhydracrylic acid at different rates. The product phenylacetaldehyde in turn was oxidized to phenylacetic acid. No hydroxylation of phenylacetic acid was detected in cell extracts, but on the basis of experiments with washed cells it is assumed that phenylacetic acid is mainly metabolized via 3-hydroxyphenylacetic acid. This latter product was subsequently hydroxylated yielding the ring-cleavage substrate homogentisate. 4-Hydroxyphenylacetic acid was also degraded via homogentisate. Ringcleavage of homogentisate gave maleylacetoacetate which was further degraded through a glutathione-dependent pathway. Homoprotocatechuate was not an intermediate in the metabolism of dl-phenylhydracrylic acid, phenylacetic, 3- and 4-hydroxyphenylacetic acid metabolism, but it could be hydroxylated aspecifically to 2,4,5-trihydroxyphenylacetic acid by the action of the 3-hydroxyphenylacetic acid-6-hydroxylase.

Pseudomonas fluorescens lipase adsorption and the kinetics of hydrolysis in a dynamic emulsion system

To elucidate the adsorption characteristics of lipases and to study the influence of the reaction conditions on the catalytic properties of lipases, the hydrolysis of decylchloroacetate by Pseudomonas fluorescens lipase in an emulsion reactor was studied as a model system. During the reaction the droplet size distribution of the emulsion was measured on-line using a particle sizer based on light scattering. Desorption experiments revealed that, at low surface coverage, the initial rate of reaction was not influenced by either the stirring speed or the organic volume fraction. Dilution of the reaction mixture during hydrolysis did not result in a decrease in activity. Based on these results, it is assumed that under the specified conditions adsorption of Pseudomonas fluorescens lipase is quantitative and probably irreversible. Based on activity measurements and assuming that only a monolayer of lipase is active, it is calculated that at saturation the emulsion interface is covered with 3 mg lipase per m2. From these data the average interfacial area covered by one lipase molecule at saturation was calculated to be 1700-2100 A2 per molecule. The emulsion was shown to be dynamic, e.g., during hydrolysis a significant increase in interfacial area was observed as a result of a shift in droplet size distribution to smaller diameters. Experiments indicated that both the formation of decanol and the emulgating effect of the lipase account for these observations. The formation of decanol also resulted in a dramatic decrease in hydrolytic activity. Taking interfacial tension measurements into account, it is shown that decanol accumulates at the liquid-liquid interface.(ABSTRACT TRUNCATED AT 250 WORDS)

Genetic analysis of benzoate metabolism in Aspergillus niger

SummaryThe benzoate metabolism of Aspergillus niger was studied as part of a design to clone the benzoate-4-hydroxylase gene of this fungus on the basis of complementation. Filtration enrichment techniques yielded mutants defective for different steps of benzoate degradation: bph (benzoate-4-hydroxylase), phh (4-hydroxybenzoate-3-hydroxylase) and prc (protocatechuate ring cleavage) mutants. In this way the degradation pathway for benzoate, involving the formation of 4-hydroxybenzoate and 3,4-dihydroxybenzoate has been confirmed. In addition a mutant sensitive to benzoate has been found. Complementation tests in somatic diploids showed that the bph mutants belonged to two complementation groups. The major group is probably defective in the structural gene (bphA). All phh mutants tested belonged to one complementation group. The prc mutants could be divided into several groups on the basis of their growth on different aromatic substrates and on the basis of the complementation test. The phh and both bph mutations are shown to be located on different chromosomes.

Microbial metabolism of D- and L-phenylglycine by Pseudomonas putida LW-4.

A strain of Pseudomonas putida capable of utilizing both stereoisomers of phenylglycine as the sole carbon and energy source was isolated from soil. No phenylglycine racemase was detected in cells grown on either stereoisomer. In an initial reaction each steroisomer of phenylglycine was transaminated yielding phenylglyoxylate which was further metabolized via benzaldehyde to benzoate. Subsequently, benzoate was further degraded via an ortho-cleavage of catechol.

Studies on the production of (S)-(+)-solketal (2,2-dimethyl-1,3-dioxolane-4-methanol) by enantioselective oxidation of racemic solketal with Comamonas testosteroni

All strains of Comamonas testosteroni investigated here, produced quinohaemoprotein ethanol dehydrogenase (QH-EDH) when grown on ethanol or butanol, but one strain of C. acidovorans and of C. terrigena did not. Hybridization experiments showed that the gene for QH-EDH is absent in the latter two strains. Induction and properties of the QH-EDHs seem to be similar: all C. testosteroni strains produced the enzyme in its apo-form [without pyrroloquinoline quinone (PQQ)] and the levels were higher at growth at low temperature; preference for the R-enentiomer and similar selectivity was shown in the oxidation of solketal (2,2-dimethyl-1,3-dioxolane-4-methanol) by cells (supplemented with PQQ); the fragment of the qhedh gene gave high hybridization with the DNA of the C. testosteroni strains. Experiments with C. testosteroni LMD 26.36 revealed that the organism is well suited for production of (S)-solketal: it shows an adequate enantioselectivity (E value of 49) for the oxidation of racemic solketal; the conversion rate of (R)-solketal is only 3.5 times lower than that of ethanol; the optimal pH for conversion (7.6) is in a region where solketal has sufficient chemical stability; separation of the remaining (S)-solketal from the acid formed is simple; induction of QH-EDH, the sole enzyme responsible for the oxidation of (R)-solketal, occurs during growth on ethanol or butanol so that the presence of solketal (inhibitory for growth) is not required; production of active cells and the conversion step can be integrated into one process, provided that PQQ and solketal addition occur at the appropriate moment; the conversion seems environmentally feasible. However, since high concentrations of solketal inhibit respiration via QH-EDH, further investigations on the mechanism of inhibition and the stability of the enzyme might be rewarding as it could lead to application of higher substrate concentrations with consequently lower down-stream processing costs.