Synthesis of dihydroxynaphthalene isomers by microbial oxidation of 1- and 2-naphthol

The mutant strain Pseudomonas fluorescens TTC1 (NCIMB 40605), derived from the naphthalene-degrading Pseudomonas fluorescens N3 (NCIMB 40530), was used for the oxidation of 1- and 2-naphthols to give different isomers of dihydroxynaphthalene. The oxidation reactions proceed through the formation of dihydrodiol intermediates, which are too unstable to be isolated, since they spontaneously eliminate water to give the fully aromatic dihydroxynaphthalenes. The high regioselectivity of the dehydration reaction was confirmed by the study of the acid-catalysed aromatization of a series of stable monosubstituted naphthalene cis-1,2-dihydrodiols. Received: 24 March 1997 / Received revision: 6 June 1997 / Accepted: 7 June 1997     

Transformation of tetrachloroethene in an upflow anaerobic sludgeblanket reactor

  Reductive dechlorination of tetrachloroethene was studied in a mesophilic upflow anaerobic sludge blanket reactor. Operating the reactor in batch mode the dynamic transformation of tetrachloroethene, trichloroethene and dichloroethene (DCE) was monitored. Tetrachloroethene was reductively dechlorinated to trichloroethene, which again was dechlorinated at the same rate as DCE was produced. DCE showed a lag period of 40 h before transformation was observed. During normal reactor operation trans-1,2-DCE was the major DCE isomer, followed by cis-1,2-DCE. Small amounts of 1,1-DCE but no vinyl chloride were detected. When the influent tetrachloroethene concentration was increased from 4.6 μM to 27 μM, the transformation rate increased, indicating that the system was not saturated with tetrachloroethene. The main organic component in the effluent was acetate, indicating that the aceticlastic methane-producing bacteria were inhibited by the chlorinated ethenes. Received: 29 July 1996 / Received revision: 13 September 1996 / Accepted: 13 September 1996     

Production of methoxyphenol-type natural aroma chemicals by biotransformation of eugenol with a new Pseudomonas sp.

In our screening program for microorganisms that are able to metabolize eugenol, the main component of the essential oil of the clove tree Syzigium aromaticum (sy. Eugenia cariophyllus), we found a new Pseudomonas sp. that produces several substituted methoxyphenols when eugenol is fed to the culture. A taxonomic characterization of this new organism has been performed. Examples of the biotransformation products, produced in high amounts, were vanillic acid with 3.25 g/l within 99 h, ferulic acid with 5.8 g/l within 75 h and coniferyl alcohol with 3.22 g/l within 47.5 h. By changing the culture conditions the ratio of the different metabolites could be varied. Based on these results a scheme for the degradation of eugenol by this strain has been established. Received: 1 April 1996 / Received revision: 24 June 1996 / Accepted: 1 July 1996     

Substrate selectivity of various lipases in the esterification of cis- and trans-9-octadecenoic acid

The substrate selectivity of numerous commercially available lipases from microorganisms, plants and animal tissue towards 9-octadecenoic acids with respect to the cis/trans configuration of the CC double bond was examined by the esterification of cis- and trans-9-octadecanoic acid (oleic and elaidic acid respectively) with n-butanol in n-hexane. A great number of lipases studied, e.g. those from Pseudomonas sp., porcine pancreas or Carica papaya, were unable to discriminate between the isomeric 9-octadecenoic acids. However, lipases from Candida cylindracea and Mucor miehei catalysed the esterification of oleic acid 3–4 times faster than the corresponding reaction of elaidic acid and therefore have a high preference for the cis isomer. Of all biocatalysts examined, only recombinant lipases from Candidaantarctica favoured elaidic acid as substrate. While the preference of Candida antarctica lipase B for the trans isomer was quite low, Candida antarctica lipase A had an extraordinary substrate selectivity and its immobilized enzyme preparation [Chirazyme L-5 (3) from Boehringer] esterified elaidic acid about 15 times faster than oleic acid. Received: 29 October 1998 / Received revision: 18 December 1998 / Accepted: 21 December 1998     

Stimulatory effect of growth in the presence of alcohols on biotransformation of penicillin G into cephalosporin-type antibiotics by resting cells of Streptomyces clavuligerus NP1

Growth of Streptomyces clavuligerus NP1 in the presence of methanol or ethanol resulted in a marked increase in production of cephalosporin(s) from penicillin G by resting cells. The mycelium produced in alcohol-supplemented medium was fragmented and dispersed as compared with growth in control medium. HPLC analysis showed that at least two products were present in the biotransformation supernatant fluid after 1 h incubation. One of them has been identified as deacetoxycephalosporin G (DAOG). Received: 9 December 1998 / Received revision: 29 March 1999 / Accepted: 16 April 1999     

Acetate enhances solvent production and prevents degeneration in Clostridium beijerinckii BA101

Addition of sodium acetate to chemically defined MP2 medium was found to increase and stabilize solvent production by Clostridium beijerinckii BA101, a solvent-hyperproducing mutant derived from C. beijerinckii NCIMB 8052. C. beijerinckii BA101 demonstrated a greater increase in solvent production than C. beijerinckii NCIMB 8052 when sodium acetate was added to MP2 medium. In 1-l batch fermentations, C. beijerinckii BA101 produced 32.6 g/l total solvents, with butanol at 20.9 g/l, when grown in MP2 medium containing 60 mM sodium acetate and 8% glucose. To our knowledge, these values represent the highest solvent and butanol concentrations produced by a solventogenic Clostridium strain when grown in batch culture. Received: 29 September 1998 / Received revision: 13 February 1999 / Accepted: 26 February 1999     

The lamellar settler – a low-cost alternative for separating the micro-alga Chlorella vulgaris from a cultivation broth?

Micro-algae, especially Chlorella vulgaris, produce a range of high-value substances and the biomass itself is used for purposes such as feeding in aquaculture. A lamellar settler was designed and built. Its suitability as a low-cost alternative to separate C. vulgaris was investigated. The settler operated semicontinuously in a laboratory photoreactor plant (total volume 9 l). A clearing of 30%–35% and a 50% increase in harvest outflow concentration were observed. The scaled up data for design and construction of a settler for a 200-l production plant were elaborated. Received: 25 September 1996 / Received revision: 10 December 1996 / Accepted: 15 December 1996     

Depolymerization of low-rank coal by extracellular fungal enzyme systems. III.In vitro depolymerization of coal humic acids by a crude preparation of manganese peroxidase from the white-rot fungus Nematoloma frowardii b19

The in vitro depolymerization of humic acids derived from German lignite (low-rank coal, brown coal) was studied using a manganese peroxidase preparation from the white-rot fungus Nematoloma frowardii b19. The H₂O₂ required was continuously generated by glucose oxidase. Mn peroxidase depolymerized high-molecular-mass humic acids by forming fulvic-acid-like compounds. The depolymerization process was accompanied by the decolorization of the dark-brown humic acid fraction soluble in alkaline solutions (decrease in absorbance at 450 nm) and by the yellowish coloring of the fraction of acid-soluble fulvic-acid-like compounds (increase in absorbance at 360 nm). The Mn peroxidase of N. frowardii b19 has been proved to be highly stable; even after an in vitro reaction time of 7 days in the presence of humic acids, less than 10% loss in total oxidizing activity was detectable. Received: 16 September 1996 / Received revision: 16 December 1996 / Accepted: 20 December 1996     

Isolation of isoflavones from soy-based fermentations of the erythromycin-producing bacterium Saccharopolyspora erythraea

A search for an abundant and economical source of isoflavones, particularly genistein, led to the discovery that the erythromycin-producing organism Saccharopolyspora erythraea also produces this promising new cancer-prevention agent. Erythromycin fermentation is a large-scale, soybean-based process used world-wide for the commercial production of this medically important antibiotic. Results from this study indicate that genistin (the glucoside form of genistein), which is added to the fermentation in the soybean media, was converted to genistein through the action of a β-glucosidase produced by the organism. Genistein was co-extracted with erythromycin from the fermentation broth, then separated from erythromycin during the second step of the purification process for the production of erythromycin. Received 10 September 1996 / Received revision: 22 November 1996 / Accepted: 7 December 1996     

Isolation and characterization of highly (R)-specific N-acetyl-1-phenylethylamine amidohydrolase, a new enzyme from Arthrobacter aurescens AcR5b

A new amidohydrolase deacetylating several N-acetyl-1-phenylethylamine derivatives (R)-specifically was found in Arthrobacter aurescens AcR5b. The strain was isolated from a wet haystack by enrichment culture with (R)-N-acetyl-1-phenylethylamine as the sole carbon source. (R) and (S )-N-acetyl-1-phenylethylamine do not serve as inducers for acylase formation. By improving the growth conditions the enzyme production was increased 47-fold. The amidohydrolase was purified to homogeneity leading to a 5.2-fold increase of the specific activity with a recovery of 67%. A molecular mass of 220 kDa was estimated by gel filtration. Sodium dodecyl sulfate/polyacrylamide gel electrophorosis shows two subunits with molecular masses of 16 kDa and 89 kDa. The optimum pH and temperature were pH 8 and 50 °C, respectively. The enzyme was stable in the range of pH 7–9 and at temperatures up to 30 °C. The enzyme activity was inhibited by Cu²⁺, Co²⁺, Ni²⁺, and Zn²⁺, and this inhibition was reversed by EDTA.M Received: 20 September 1996 / Received version: 23 December 1996 / Accepted: 30 December 1996     

Production, purification, and characterization of a highly enantioselective (S )-N-acetyl-1-phenylethylamine amidohydrolase from Rhodococcus equi Ac6

Rhodococcus equi Ac6 was found to express an inducible (S )-specific N-acetyl-1-phenylethylamine amidohydrolase. Optimal bacterial growth and amidohydrolase expression were both observed around pH 6.5. Purification of the enzyme to a single band in a Coomassie-blue-stained sodium dodecyl sulfate/polyacrylamide gel (SDS-PAGE) was achieved by ammonium sulfate precipitation of R. equi Ac6 crude extract and column chromatographies on Fractogel TSK Butyl-650(S) and Superose 12HR. At pH 7.0 and 30 °C the amidohydrolase had a half-life of around 350 days; at 44 °C it was only 10 min. Except for Ni²⁺ and, to some extent, Zn²⁺ and Co²⁺, the enzyme was neither strongly influenced by metal cations nor by chelating agents, but was inhibited by 95% at 0.1 mM phenylmethylsulfonyl fluoride. The molecular mass of the native enzyme was estimated to be 94 kDa by gel filtration and 50 kDa by SDS-PAGE, suggesting a dimeric structure. Specificity experiments revealed a spectrum of related N-acetylated compounds being hydrolyzed with variable enantiomeric selectivities. Received: 20 September 1996 / Received revision: 23 December 1996 / Accepted: 30 December 1996     

Molecular mass of poly[(R )-3-hydroxybutyric acid] produced in a recombinant Escherichia coli

 Poly[(R)-3-hydroxybutyric acid] (PHB) was produced at 37 °C by a recombinant Escherichia coli harboring the Alcaligenes eutrophus biosynthesis phbCAB genes in Luria-Bertani media containing glucose at 10–30 g/l at different pH values and the time-dependent changes in the molecular mass of PHB were studied. PHB polymers accumulated within cells while glucose was present in the medium. The number-average molecular mass of PHB decreased with time during the course of PHB accumulation, and the values for PHB were markedly dependent on the cultivation conditions of the E. coli, ranging from 0.5 MDa to 20 MDa. Under specific conditions (pH 6.0), E. coli produced PHB with an extremely high molecular mass (20 MDa). It has been suggested that a chain-transfer agent is generated in E. coli cells during the accumulation of PHB. Received: 18 July 1996 / Received revision: 4 November 1996 / Accepted: 4 November 1996     

Screening for fungi intensively mineralizing 2,4,6-trinitrotoluene

Within a screening program, 91 fungal strains belonging to 32 genera of different ecological and taxonomic groups (wood- and litter-decaying basidiomycetes, saprophytic micromycetes) were tested for their ability to metabolize and mineralize 2,4,6-trinitrotoluene (TNT). All these strains metabolized TNT rapidly by forming monoaminodinitrotoluenes (AmDNT). Micromycetes produced higher amounts of AmDNT than did wood- and litter-decaying basidiomycetes. A significant mineralization of [¹⁴C]TNT was only observed for certain wood- and litter-decaying basidiomycetes. The most active strains, Clitocybula dusenii TMb12 and Stropharia rugosa-annulata DSM11372 mineralized 42 % and 36 % respectively of the initial added [¹⁴C]TNT (100 μM corresponding to 4.75 μCi/l) to ¹⁴CO₂ within 64 days. Micromycetes (deuteromycetes, ascomycetes, zygomycetes) proved to be unable to mineralize [¹⁴C]TNT significantly. Received: 8 August 1996 / Received revision: 16 December 1996 / Accepted: 20 December 1996     

Pyrazine production by Bacillus subtilis in solid-state fermentation on soybeans

2,5-Dimethylpyrazine (2,5-DMP) and tetramethylpyrazine (TTMP) were produced using Bacillus subtilis IFO 3013 grown on soybeans. Solid-state cultivations were carried out either in 100-ml bottles or in a fixed-bed column reactor, both systems being at 27 °C. Optimization studies showed that the best way to produce the two above aroma compounds involved two separate processes. 2,5-DMP was obtained using soybeans enriched with 75 g threonine/kg initial dry weight (i.d.w.), giving 0.85 g metabolite/kg i.d.w. after 6 days. TTMP production involved addition of 90 g/kg i.d.w. acetoin to soybeans, and 2.5 g/kg i.d.w. was recovered after 14 days. These results demonstrated the suitability of solid-state cultivation for production of high-added-value compounds. Received: 30 September 1996 / Received revision: 23 December 1996 / Accepted: 30 December 1996     

Formation of benzaldehyde by Pseudomonas putida ATCC 12633

Aromatic and heterocyclic aldehydes may be produced by the mandelate pathway of Pseudomonas putida ATCC 12633 via the biotransformation of benzoyl formate and substrate analogues. Under optimised biotransformation conditions (37 °C, pH 5.4) and with benzoyl formate as a substrate, benzaldehyde may be accumulated with yields above 85%. Benzaldehyde is toxic to P. putida ATCC 12633; levels above 0.5 g/l (5 mM) reduce the biotransformation activity. Total activity loss occurs at an aldehyde concentration of 2.1 g/l (20 mM). To overcome this limitation, the rapid removal of the aldehyde is desirable via in situ product removal. The biotransformation of benzoyl formate (working volume 1 l) without in situ product removal accumulates 2.1 g/l benzaldehyde. Benzaldehyde removal by gas stripping produces a total of 3.5 g/l before inhibition. However, the most efficient method is solid-phase adsorption using activated charcoal as the sorbant, this allows the production of over 4.1 g/l benzaldehyde. Addition of bisulphite as a complexing agent causes inhibition of the biotransformation and bisulphite is therefore is not suitable for in situ product removal. Received: 16 March 1998 / Received revision: 20 May 1998 / Accepted: 21 May 1998     

High-density Escherichia coli cultures for continuous l(−)-carnitine production

The use of a biological procedure for l-carnitine production as an alternative to chemical methods must be accompanied by an efficient and highly productive reaction system. Continuous l-carnitine production from crotonobetaine was studied in a cell-recycle reactor with Escherichia coli O44 K74 as biocatalyst. This bioreactor, running under the optimum medium composition (25 mM fumarate, 5 g/l peptone), was able to reach a high cell density (26 g dry weight/l) and therefore to obtain high productivity values (6.2 g l-carnitine l⁻¹ h⁻¹). This process showed its feasibility for industrial l-carnitine production. In addition, resting cells maintained in continuous operation, with crotonobetaine as the only medium component, kept their biocatalytic capacity for 4 days, but the biotransformation capacity decreased progressively when this particular method of cultivation was used. Received: 10 December 1998 / Received revision: 19 February 1999 / Accepted: 20 February 1999     

Evidence for diverse oxidations in the catabolism of toluene by Rhodococcus rhodochrous strain OFS

Rhodococcus rhodochrous strain OFS grew on toluene as a sole source of carbon and energy with a maximum growth rate of 0.011 h⁻¹. Initial reaction products were extracted, derivatized and identified by GC-MS. Oxygen consumption studies indicated that OFS grown on an aliphatic substrate required an induction period before oxidizing toluene. OFS grown on toluene transformed an array of aromatic ground water pollutants including styrene, ethylbenzene and chlorobenzene. Products of these transformations were identified. The sole product of chlorobenzene biotransformation was 4-chlorophenol. Products from toluene oxidation included 3- and 4-methylcatechol as well as benzyl alcohol, p-cresol and cis-toluene dihydrodiol. The identification of these and the products of other aromatic substrate conversions affirm that oxidation occurred on the functional group as well as directly on the aromatic nucleus. Received: 23 July 1999 / Received revision: 4 October 1999 / Accepted: 16 October 1999     

Pilot-scale production of butanol by Clostridium beijerinckii BA101 using a low-cost fermentation medium based on corn steep water

To improve the economic competitiveness of the acetone/butanol/ethanol fermentation process, glucose/corn steep water (CSW) medium was used on a pilot scale for the production of solvents. The production of butanol by the Clostridium beijerinckii NCIMB 8052 parent strain and the solvent-hyperproducing BA101 mutant was compared. In a 20-l fermentation using 5% glucose/CSW medium,  C. beijerinckii 8052 produced 8.5 g butanol/l and 5 g acetone/l, while  C. beijerinckii BA101 produced 16 g butanol/l and 7.5 g acetone/l. Further studies were carried out on a larger scale using an optimized 6% glucose/CSW medium. In a 200-l pilot-scale fermentor,  C. beijerinckii 8052 produced 12.7 g butanol/l and 6 g acetone/l following 96 h of fermentation.  C. beijerinckii BA101 produced 17.8 g/l and 5.5 g/l butanol and acetone respectively, following 130 h of fermentation. These results represent a 40% increase in final butanol concentration by the C. beijerinckii BA101 mutant strain when compared to the 8052 parent strain. The total solvents (acetone, butanol, and ethanol) produced by C. beijerinckii NCIMB 8052 and BA101 in a 200-l fermentation were 19.2 g/l and 23.6 g/l respectively. This is the first report of pilot-scale butanol production by the solvent-hyperproducing C. beijerinckii BA101 mutant employing an inexpensive glucose/CSW medium. Received: 26 May 1998 / Received revision: 21 September 1998 / Accepted: 11 October 1998     

A physical assay for meiotic recombination in Coprinus cinereus

We have used the polymerase chain reaction (PCR) method to monitor meiotic recombination in the basidiomycete Coprinus cinereus. We used DNA-mediated transformation to recover strains with modifications of the trp1 locus. The modifications were designed to introduce unique PCR priming sites separated by a homologous 2.4 kb region in which crossing over could occur. We showed that exchange occurred in this region at the frequency expected for a typical region of this genome (2.4 kb should correspond to a genetic length of 0.08 cM). We also detected products resulting from crossing over in DNAs extracted from cells in meiotic prophase. The assay should be useful for monitoring exchange in mutants that cannot complete meiosis. Received: 5 September 1996 / Accepted: 1 December 1996     

Sophorose lipid fermentation with differentiated substrate supply for growth and production phases

Sophorose lipid production by Candida bombicola is a two-step process where sophorose lipids are mainly produced after a first stage of growth, ending because of nitrogen limitation. The influence of the following parameters was individually studied for both the stages of growth and of product formation with respect to final sophorose lipid production performance: pH, temperature and carbon source. Glucose and rapeseed ethyl esters were supplied individually or as a dual carbon source. The lipidic substrate was added by continuous feeding. It was found that supplying both carbon sources during the production step was crucial for obtaining a high production performance ranging from 250 g l⁻¹ to 300 g l⁻¹ or more. Controlling the feeding of rapeseed ethyl esters to avoid inhibition by fatty acids was essential for a successful scale-up of the fermentation on the industrial scale. The conditions of substrate feeding markedly affected the composition of the mixture of sophorose lipids produced, namely the extent of acetylation of the sophorose moieties and distribution of the acidic and lactonic forms. The results suggest that the physiological role of sophorose lipid production is related to the regulation of energy metabolism. Received: 26 June 1996 / Received revision: 12 December 1996 / Accepted: 15 December 1996