Production of a chiral alcohol, 1-(3,4-dihydroxyphenyl) ethanol, by mushroom tyrosinase.

1-(3,4-Dihydroxyphenyl) ethanol was produced biocatalytically for the first time using mushroom tyrosinase. 4-Ethylphenol at 1 mM was consumed over 12 min giving 0.23 mM 4-ethylcatechol and 0.36 mM (R/S)-1-(3,4-dihydroxyphenyl) ethanol (ee 0.5 %). Mushroom tyrosinase consumed 4-ethylphenol at 6.7 µmol min(-1) mg protein(-1) while the rates of formation of 4-ethylcatechol and 1-(3,4-dihydroxyphenyl) ethanol were 1.1 and 1.9 µmol min(-1) mg protein(-1). Addition of the ascorbic acid, as a reducing agent to biotransformation reactions, increased 4-ethylcatechol formation by 340 %. However, accumulation of 1-(3,4-dihydroxyphenyl) ethanol was not observed in the presence of ascorbic acid. While the 1-(3,4-dihydroxyphenyl) ethanol was racemic, it is the first chiral product produced by tyrosinase starting from a non-chiral substrate.

Biotransformation of 4-halophenols to 4-halocatechols using Escherichia coli expressing 4-hydroxyphenylacetate 3-hydroxylase.

Escherichia coli cells, expressing 4-hydroxyphenylacetate 3-hydroxylase, fully transformed 4-halogenated phenols to their equivalent catechols as single products in shaken flasks. 4-Fluorophenol was transformed at a rate 1.6, 1.8, and 3.4-fold higher than the biotransformation of 4-chloro-, 4-bromo-, and 4-iodo-phenol, respectively. A scale-up from shaken flask to a 5 L stirred tank bioreactor was undertaken to develop a bioprocess for the production of 4-substituted halocatechols at higher concentrations and scale. In a stirred tank reactor, the optimized conditions for induction of 4-HPA hydroxylase expression were at 37 °C for 3 h. The rate of biotransformation of 4-fluorophenol to 4-fluorocatechol by stirred tank bioreactor grown cells was the same at 1 and 4.8 mM (5.13 µmol/min/g CDW) once the ratio of biocatalyst (E. coli CDW) to substrate concentration (mM) was maintained at 2:1. At 10.8 mM 4-fluorophenol, the rate of 4-fluorocatechol formation decreased by 4.7-fold. However, the complete transformation of 1.3 g of 4-fluorophenol (10.8 mM) to 4-fluorocatechol was achieved within 7 h in a 1 L reaction volume. Similar to 4-fluorophenol, other 4-substituted halophenols were completely transformed to 4-halocatechols at 2 mM within a 1-2 h period. An increase in 4-halophenol concentration to 4.8 mM resulted in a 2.5-20-fold decrease in biotransformation efficiency depending on the substrate tested. Organic solvent extraction of the 4-halocatechol products followed by column chromatography resulted in the production of purified products with a final yield of between 33% and 38%.

The conversion of BTEX compounds by single and defined mixed cultures to medium-chain-length polyhydroxyalkanoate.

Here, we report the use of petrochemical aromatic hydrocarbons as a feedstock for the biotechnological conversion into valuable biodegradable plastic polymers--polyhydroxyalkanoates (PHAs). We assessed the ability of the known Pseudomonas putida species that are able to utilize benzene, toluene, ethylbenzene, p-xylene (BTEX) compounds as a sole carbon and energy source for their ability to produce PHA from the single substrates. P. putida F1 is able to accumulate medium-chain-length (mcl) PHA when supplied with toluene, benzene, or ethylbenzene. P. putida mt-2 accumulates mcl-PHA when supplied with toluene or p-xylene. The highest level of PHA accumulated by cultures in shake flask was 26% cell dry weight for P. putida mt-2 supplied with p-xylene. A synthetic mixture of benzene, toluene, ethylbenzene, p-xylene, and styrene (BTEXS) which mimics the aromatic fraction of mixed plastic pyrolysis oil was supplied to a defined mixed culture of P. putida F1, mt-2, and CA-3 in the shake flasks and fermentation experiments. PHA was accumulated to 24% and to 36% of the cell dry weight of the shake flask and fermentation grown cultures respectively. In addition a three-fold higher cell density was achieved with the mixed culture grown in the bioreactor compared to shake flask experiments. A run in the 5-l fermentor resulted in the utilization of 59.6 g (67.5 ml) of the BTEXS mixture and the production of 6 g of mcl-PHA. The monomer composition of PHA accumulated by the mixed culture was the same as that accumulated by single strains supplied with single substrates with 3-hydroxydecanoic acid occurring as the predominant monomer. The purified polymer was partially crystalline with an average molecular weight of 86.9 kDa. It has a thermal degradation temperature of 350 degrees C and a glass transition temperature of -48.5 degrees C.

Resolution of methyl nonactate by Rhodococcus erythropolis under aerobic and anaerobic conditions.

[reaction: see text]. An efficient resolution of methyl nonactate is reported by biotransformation in shake flask cultures of Rhodococcus erythropolis. The equilibrium of the reaction redox system can be manipulated by switching from aerobic to anaerobic growth, thereby generating both enantiomers of the target in excellent yield and enantiomeric purity.

High frequency transformation of the Amphotericin-producing bacterium Streptomyces nodosus.

This study has investigated DNA transformation in the Amphotericin-producing organism Streptomyces nodosus. Amphotericin B is an antifungal drug with severe side effects in humans and the availability of structural variants would aid investigations into the mode of action and cytotoxity of the drug. Analogs of related polyketide drugs have been rapidly made by genetic engineering of biosynthetic genes; however, this requires the introduction of foreign DNA into the host. Protocols for protoplast formation and regeneration were established; however, preparations were recalcitrant to DNA uptake. Electroporation-mediated methodologies also were not successful. Intergeneric conjugal transfer of DNA from E. coli demonstrated transformation efficiencies of 5 x 10(-5) exconjugants generated per recipient. Use of DNA methylation-impaired E. coli donor strains resulted in 100-fold higher transformation efficiencies, indicating that DNA methylation recognition systems are operable in the organism. This methodology will enable genetic and biochemical analysis of the gene cluster responsible for making Amphotericin B.

Community structure and antibiotic production of Streptomyces nodosus bioreactors cultured in liquid environments.

Immobilized bacteria are being assessed by industry for drug delivery, novel fermentation systems and the protection of organisms in harsh environments. Alginate bioreactors containing Streptomyces nodosus were examined for community structure, cell viability and amphotericin production under different growth conditions. When cell proliferation was encouraged, substrate hyphae were found inside the alginate matrix and within multicellular projections on the surface of the capsule. The periphery of these projections had erect and branched hyphae, morphologically identical to aerial hyphae. Antibiotic production from immobilized organisms was assessed using conditioned culture medium to eliminate the emergence of a free-dwelling population. These organisms sporulated with reduced antibiotic production compared with free-dwelling cultures. The commitment to sporulate was independent of a surface but dependent on community size and nutritional status. This is the first report of the sporulation of S. nodosus in liquid cultures and description of the multicellular community the organism adopts at a solid-liquid interface.

A second generation snp-derived Escherichia coli-Streptomyces shuttle expression vector that is generally transferable by conjugation.

An Escherichia coli-Streptomyces shuttle vector (pJN100) was constructed, by inserting an origin of transfer (oriT), derived from the E. coli broad host range plasmid RK2, into pANT1202, a high-copy-number vector for gene expression in Streptomyces. The resulting conjugably transferable vector contains the pANT1202-derived SnpR (LysR-like protein) activated snpA promoter that drives strong heterologous expression of proteins. We initially demonstrated that plasmid pJN100 was transferred with high frequency (10(-5-7) exconjugants per recipient) into several Streptomyces strains that were refractory to transformation by other means. Plasmid pJN100 was also shown to be stable in E. coli and Streptomyces. We confirmed functional protein expression by using a pJN100 derivative to complement a mutant of Streptomyces griseus with a disrupted chromosomal copy of the gene nonM, a gene encoding an essential reductase in the nonactin biosynthesis gene cluster. High levels of protein expression were confirmed using Western blotting to assess the production of the serine esterase NonR, an enzyme responsible for nonactin resistance in the nonactin producer S. griseus.

Amplification of DNA encoding entire type I polyketide synthase domains and linkers from streptomyces species.

Polyketides are a group of bioactive compounds from bacteria, plants, and fungi. To increase the availability of analogs for testing, the active sites of polyketide synthases are often substituted with homologous domains having altered substrate specificities. This study reports the design of polymerase chain reaction primers that enables isolation of entire active site domains from type I polyketide synthases with native interdomain linkers. This bypasses the need for further genetic screening to obtain functional units for use in genetic engineering. This is especially important in bioprospecting projects exploring new environments for bioresources.