Isolation of an Acinetobacter sp. ST-550 which produces a high level of indigo in a water-organic solvent two-phase system containing high levels of indole

Acinetobacter sp. strain ST-550 was isolated from fumus soil as an efficient indigo producer in the presence of organic solvent. The minimum inhibitory concentration of indole was 0.4 mg/ml for ST-550. ST-550 produced only a small amount of indigo (less than 0.01 microg/ml) when grown in the presence of indole at concentrations of 0.05 to 0.3 mg/ml without any organic solvent. However. ST-550 produced indigo effectively when grown in the presence of a large volume of diphenylmethane and a high level of indole: optimized conditions were 3 ml of a medium containing 0.3 ml diphenylmethane and 2.7 mg indole. Under these conditions, ST-550 produced 0.88 mg indigo (292 microg/mI medium).     

Stability of hydrolytic enzymes in water-organic solvent systems

The effects of organic solvents on the stabilities of bovine pancreas trypsin, chymotrypsin, carboxypeptidase A and porcine pancreas lipase were studied. Water-miscible solvents (ethanol, acetonitrile, 1,4-dioxane and dimethyl sulfoxide) and water-immiscible solvents (ethyl acetate and toluene) were used in 100 mM phosphate buffer (pH 7.0) or 100 mM Tris/HCl buffer (pH 7.0) in concentrations of 20–80% (v/v). All hydrolytic enzymes studied were inactivated by mixtures containing dimethyl sulfoxide at higher concentrations. Trypsin and carboxypeptidase A resisted solvent mixtures containing acetonitrile, 1,4-dioxane and ethanol. They preserved more than 80% of their starting activities during 20-min incubations. The activities of lipase and chymotrypsin decreased with increasing concentration of water-miscible polar organic solvents, but at higher concentrations (80%) 70–90% of the activity remained. In mixtures with water-immiscible solvents, the decrease in activity of carboxypeptidase A was pronounced. Trypsin and chymotrypsin underwent practically no loss in activity in the presence of toluene or ethyl acetate. In respect of stability, the polar solvent proved to be more favorable for lipase. These results suggest that the conformational stabilities of hydrolytic enzymes are highly dependent on the solvent-protein interactions and the enzyme structure.     

Biocatalytic oxidation of bisphenol A in a reverse micelle system using horseradish peroxidase

Horseradish peroxidase (HRP) was used to catalyze the oxidation of bisphenol A (BPA) in a reverse micelle system consisting of water, sodium bis(2-ethylhexyl)sulfosuccinate (AOT) as the surfactant, and n-octane as the organic solvent phase. In order to achieve maximal BPA transformation, a water-to-surfactant molar ratio greater than 15 was required, above which no further increase in conversion was observed. BPA transformation was catalyzed in the reverse micelle system over a pH range of 6-9 with an optimum at pH 7 and was enhanced with increasing temperatures up to 40 degrees C. The stoichiometric ratio of moles of bisphenol A transformed per mole of peroxide consumed was 0.46 when the initial BPA concentration was 0.01 mM, which is significantly less than the theoretical value of 2 based on the known catalytic cycle of the enzyme. However, the stoichiometric ratio increased and approach the theoretical value with higher BPA concentrations. Over the course of the catalytic reaction, the enzyme became inactivated. Hydrogen peroxide strongly inhibited the enzyme and, thus, when the oxidant was present in quantities in excess of the stoichiometric amount, BPA transformation was significantly reduced.     

Glycosidases in organic solvents: I. Alkyl-β-glucoside synthesis in a water-organic two-phase system

A low-water organic solvent two-phase system suitable for glycosylation of hydrophobic substrates is described. Almond β-glucosidase adsorbed on polymeric supports has been shown to catalyse alkyl-β-glucoside synthesis via a transferase reaction or through direct condensation of the glucosidic bond. High concentrations of glucosyl donors were present in the aqueous phase, while water-immiscible primary alcohols, which form the organic phase, served as acceptors of glucose. Reaction yield appeared to be thermodynamically controlled. The influence of various support materials, glucosyl donors, and glucosyl acceptors on reaction rate and product yield was investigated.     

Alterations to the catalytic properties of polyphenoloxidase in detergentless microemulsions and ternary water-organic solvent mixtures

Summary The catalytic properties of mushroom polyphenoloxidase could be substantially altered by entrapment into hexane- and toluene-based microemulsions stabilized with isopropanol. The fast irreversible inactivation and drastic substrate inhibition of the enzyme were significantly reduced in detergentless microemulsions in comparison to conventional aqueous media. Similar changes in the catalytic behavior of polyphenoloxidase were observed in the normal ternary solutions of hexane-(toluene)-isopropanol-water, and in the H-bonded aggregates of isopropanol and water in toluene, but not in hexane.     

Rates of deactivation processes of indole derivatives in water-organic solvent mixtures--application to tryptophyl fluorescence of proteins.

The fluorescence quantum yield and the fluorescence decay of indole, 3-methylindole, 1-methylindole and N-acetyltryptophanamide have been measured in different water-dioxane mixtures. For the first three derivatives, the fluorescence decays were found independent of the emission wavelength and were analyzed as single exponential functions. In the case of N-methylindole the rate of the non radiative deactivation processes knr increased linearly with the molar fraction of dioxane whereas for indole and scatole the variation of knr was biphasic. This behaviour can be explained by two excited state deactivations of these non N-methylated compounds in water and high water content mixtures; one of these deactivation processes occuring through an hydrogen bond between the N-H group and a water molecule. The rate of non radiative deactivation of N-acetyltryptophanamide was dominated by the internal quenching involving the intramolecular carbonyl. The rate of the radiative deactivation process kF of these four compounds increased linearly with the wavenumber of the fluorescence spectrum maximum. Data relative to the three non N-methylated derivatives fell practically on the same straight line. Data from other works have been gathered in order to check if a similar relation between the intrinsic kF and vF values can exist for the tryptophyl fluorescence emission of proteins.     

Stabilization and activation of alpha-chymotrypsin in water-organic solvent systems by complex formation with oligoamines

Formation of enzyme-oligoamine complexes was suggested as an approach to obtain biocatalysts with enhanced resistance towards inactivation in water-organic media. Complex formation results in broadening (by 20-40% v/v ethanol) of the range of cosolvent concentrations where the enzyme retains its catalytic activity (stabilization effect). At moderate cosolvent concentrations (20-40% v/v) complex formation activates the enzyme (by 3-6 times). The magnitude of activation and stabilization effects increases with the number of possible electrostatic contacts between the protein surface and the molecules of oligoamines (OA). Circular dichroism spectra in the far-UV region show that complex formation stabilizes protein conformation and prevents aggregation in water-organic solvent mixtures. Two populations of the complexes with different thermodynamic stabilities were found in alpha-chymotrypsin (CT)-OA systems depending on the CT/OA ratio. The average dissociation constants and stoichiometries of both low- and high-affinity populations of the complexes were estimated. It appears that it is the low-affinity sites on the CT surface that are responsible for the activation effect.     

Prediction of penicillin V acylase stability in water-organic co-solvent monophasic systems as a function of solvent composition

Hydrolytic activity of penicillin V acylase (EC 3.5.1.11) can be improved by using organic cosolvents in monophasic systems. However, the addition of these solvents may result in loss of stability of the enzyme. The thermal stability of penicillin V acylase from Streptomyces lavendulae in water-organic cosolvent monophasic systems depends on the nature of the organic solvent and its concentration in the media. The threshold solvent concentration (at which half enzymatic activity is displayed) is related to the denaturing capacity of the solvent. We found out linear correlations between the free energy of denaturation at 40 degrees C and the concentration of the solvent in the media. On one hand, those solvents with logP values lower than -1.8 have a protective effect that is enhanced when its concentration is increased in the medium. On the other hand, those solvents with logP values higher than -1.8 have a denaturing effect: the higher this value and concentration, the more deleterious. Deactivation constants of PVA at 40 degrees C can be predicted in any monophasic system containing a water-miscible solvent.     

The inhibition of mitochondrial DNA replication in vitro by the metabolites of benzene, hydroquinone and p-benzoquinone

Rat liver mitochondria incubated with the metabolites of benzene, p-benzoquinone or 1,2,4-benzenetriol, showed a dose-dependent inhibition of [3H]dTTP incorporation into mtDNA with median inhibitory concentrations of 1 mM for each compound. Benzene and the metabolites phenol, catechol and hydroquinone did not inhibit at concentrations up to 10 mM. Similarly, incubation of p-benzoquinone or hydroquinone with rabbit bone marrow mitochondria showed a dose-dependent inhibition of mtDNA synthesis with 50% inhibition at 1 mM and 10 mM, respectively. That these metabolites inhibit mitochondrial replication was evidenced by the fact that [3H]dTTP incorporation into characteristic 38S, 27S and 7S mitochondrial replication intermediates was decreased by the quinones, as analyzed on 5-20% neutral sucrose velocity gradients. p-Benzoquinone, hydroquinone and 1,2,4-benzenetriol inhibited the activity of partially purified rat liver mtDNA polymerase gamma using either activated calf thymus DNA or poly(rA) X p(dT)12-18 as primer/template, with 50% inhibitory concentrations of 25 microM, 25 microM and 180 microM, respectively. Preincubation of the metabolites with polymerase gamma or primer/template, followed by removal of the unreacted metabolite by gel filtration, indicated that inhibition resulted from interaction of the metabolites with the enzyme, rather than with the template. Binding appeared to involve a sulfhydryl residue on the enzyme since the binding of [14C]hydroquinone was prevented by N-ethylmaleimide. The ability of hydroquinone or p-benzoquinone to inhibit binding of [14C]hydroquinone to the enzyme suggests that the compounds bind to a common site or are converted to a common intermediate. Inhibition of, or changes in, replication in mitochondria of bone marrow cells by hydroquinone and p-benzoquinone may explain the changes in the mitochondrial genome observed in marrow stem cells in acute myelogenous leukemia and may suggest a mechanism for benzene leukemogenesis.     

A statistical mechanical theory of unfolding of globular proteins induced by preferential binding of solvent components in water-organic solvent systems

A statistical mechanical model was developed for use in connection with the problem of preferential binding of solvent components to proteins and of conformational transition in water-organic solvent systems. The model is a statistical one for the conformational transition of globular proteins induced by the adsorption of solutes in the solution, considered as a nearest-neighbor problem in statistical mechanics. Although a few illustrative examples are given, the actual interpretations of the experimental data using this theory are reserved for a later paper.     

Complete anaerobic oxidation of hydroquinone by Desulfococcus sp. strain Hy5: indications of hydroquinone carboxylation to gentisate

The sulfate-reducing strain Hy5 was able to grow with hydroquinone as sole source of carbon and energy. In experiments with dense cell suspensions, several indications were found that gentisate was the first intermediate in anaerobic degradation of hydroquinone: (1) degradation of hydroquinone was accelerated by addition of bicarbonate; (2) cell suspensions grown with hydroquinone oxidized gentisate at a rate similar to that of suspensions grown with gentisate, whereas the latter were not able to degrade hydroquinone in the presence of chloramphenicol; (3) in SDS-PAGE analysis of cell-free extracts of strain Hy5, two additional protein bands were found after growth with hydroquinone that were not detected in cells grown with gentisate, probably representing a hydroquinone carboxylating enzyme. A corresponding enzyme activity could not be detected. In cell-free extracts of hydroquinone-grown strain Hy5, the specific acyl-CoA ligase activity with gentisate as substrate was detected at 70 nmol x mg^-1 x min^-1. Gentisyl-CoA was enzymatically reduced to several unidentified nonaromatic products in the presence of dithionite-reduced methyl viologen.     

Mechanistic aspects of the tyrosinase oxidation of hydroquinone

Contradictory reports on the behaviour of hydroquinone as a tyrosinase substrate are reconciled in terms of the ability of the initially formed ortho-quinone to tautomerise to the thermodynamically more stable para-quinone isomer. Oxidation of phenols by native tyrosinase requires activation by in situ formation of a catechol formed via an enzyme generated ortho-quinone. In the special case of hydroquinone, catechol formation is precluded by rapid tautomerisation of the ortho-quinone precursor to catechol formation.     

Biotransformation of 2-phenylethanol to phenylacetaldehyde in a two-phase fed-batch system

Phenylacetaldehyde (PA) can be produced by the oxidation of 2-phenylethanol (PE) through biotransformation. In order to prevent substrate and product inhibitions and the transformation of the PA to phenylacetic acid (PAA), utilization of a two-phase system is very attractive. Gluconobacter oxydans B-72 was used as the microorganism and iso-octane as the solvent. The effect of initial substrate concentration on the PA production was investigated in single- and two-phase systems. In the single-phase system, substrate inhibition occurred above 5 g/l, and in the two-phase system, above 7.5 g/l. Substrate inhibition kinetics were also studied in the two-phase system and kinetic constants were determined as r_max=0.64 g/l min, K_M=8.15 g/l, K_PA=2.5 g/l. Because it was observed that two-phase system is insufficient to remove the substrate inhibition effect, fed-batch operation was utilised in this study. For 7.5 g/l of PE, 1.65, 3.85, and 7.35 g/l of PA were obtained in the single-phase, two-phase, and two-phase three fed-batch systems, respectively. Effect of biotransformation time, initial substrate concentration, agitation speed, and fed-batch number on the PA production was investigated in a two-phase fed-batch system by the response surface methodology (RSM). The optimum values were found as 3 fed-batch number, 2.75 g/l initial substrate concentration, 150 rpm agitation speed, and 65 min of one batch biotransformation time. In order to verify these results, an experiment was performed at these optimum conditions and 7.10 g/l of PA concentration was obtained.     

Purification and characterization of a feruloyl esterase from Fusarium oxysporum catalyzing esterification of phenolic acids in ternary water-organic solvent mixtures

An extracellular feruloyl esterase (FAE-II) from the culture filtrates of Fusarium oxysporum F3 was purified to homogeneity by SP-Sepharose, t-butyl-HIC and Sephacryl S-200 column chromatography. The protein corresponded to molecular mass and pI values of 27 kDa and 9.9, respectively. The enzyme was optimally active at pH 7 and 45 degrees C. The purified esterase was fully stable at pH 7.0-9.0 and temperature up to 45 degrees C after 1 h incubation. Determination of k(cat)/K(m) revealed that the enzyme hydrolysed methyl sinapinate 6, 21 and 40 times more efficiently than methyl ferulate, methyl coumarate and methyl caffeate, respectively. The enzyme was active on substrates containing ferulic acid ester linked to the C-5 but inactive to the C-2 positions of arabinofuranose such as 4-nitrophenyl 5-O-trans-feruloyl-alpha-L-arabinofuranoside and 4-nitrophenyl 2-O-trans-feruloyl-alpha-L-arabinofuranoside. In the presence of Sporotrichum thermophile xylanase, there was a significant release of ferulic acid from destarched wheat bran by FAE-II, indicating a synergistic interaction between FAE-II and S. thermophile xylanase. FAE-II by itself could release only little ferulic acid from destarched wheat bran. The potential of FAE-II for the synthesis of various phenolic acid esters was tested using as a reaction system a surfactantless microemulsion formed in ternary mixture consisting of n-hexane, 1-propanol and water.     

Polymer-polymer organic solvent two-phase system: A new type of reaction medium for bioorganic synthesis

Mixing solutions of polymers dissolved in chloroform resulted in turbid solutions that parted into two separate phases upon standing. Each phase consisted primarily of one of the two polymers and contained only small amounts of the other. An enzyme (alpha-chymotrypsin) added to the two-phase system partitioned preferentially to one of the phases; this was observed with native enzyme and with enzyme associated with one of the polymers through non-convalent interactions. Under the conditions studied, alpha-chymotrypsin was active and expressed even higher activity and stability than native enzyme added to the organic solvent without polymer. An emulsion was easily formed on mixing with small droplets of one of the phases suspended in the other phase. By operating with the enzyme in the emulsion, a very attractive system for carrying out enzyme-catalyzed conversions was created. Short diffusion distances and minimized steric hindrance are two characteristics of such systems. At the conclusion of the reaction, stirring/mixing was ceased and, after phase separation, it was possible to recover the enzyme as well as the product, under ideal conditins, from different phases. The enzyme was then reused. (c) 1994 John Wiley & Sons, Inc.