Cell growth and enzyme synthesis of a mutant of Arthrobacter sp. (DSM 3747) used for the production of L-amino acids from D,L-5-monosubstituted hydantoins.

A microorganism with the ability to form L-tryptophan from D,L-5-(3-indolyl-methyl)hydantoin (D,L-5-IMH) was isolated and identified as Arthrobacter sp. (DSM 3747). After isolation of a mutant with high tryptophan production activity but low tryptophan degradation, cultural conditions were optimized to achieve high amounts of biomass with good specific activities concerning the enzymatic hydantoin-cleaving reactions. The ability of the microorganism to perform these bioconversions was found to be inducible by D,L-5-IMH as well as to be dependent on the presence of Mn2+. The highest specific D,L-5-IMH-cleaving activity of the cells was observed in the exponential phase of growth. The addition of yeast extract to the mineral salts medium was found to be essential for obtaining biomass concentrations of about 25 g l-1 cell dry mass by bioreactor cultivations. In order to obtain a constantly high growth rate, feeding of the C-source was pO2-controlled. The inducer D,L-5-IMH had to be continuously fed to prevent a decline of the L-tryptophan-forming enzyme activities, because it was subjected to degradation with the enzymes induced and higher concentrations of D,L-5-IMH aggravated the growth significantly. The synthesis of the enzymes was also inducible, when inducer and Mn2+ were not added until the late growth phase. Using this process, the consumption of D,L-5-IMH was reduced remarkably. So, under these conditions biomass concentrations of 25 g l-1 cell dry weight with a specific enzymatic activity of 0.20 mmol g-1 h-1 (tryptophan per dry mass per time) could be obtained within 13 h. Using 1 g l-1 of the chemically modified inducer D,L-5-(3-indolylmethyl)-3-N-methylhydantoin, which was not degradable by the microorganisms, a biomass concentration of 28 g l-1 cell dry weight with a specific activity of 0.34 mmol g-1 h-1 (tryptophan per dry mass per time) could be obtained within 28 h.     

Immobilization of the hydantoin cleaving enzymes from Arthrobacter aurescens DSM 3747.

The immobilization procedure of the two industrially important hydantoin cleaving enzymes--hydantoinase and L-N-carbamoylase from Arthrobacter aurescens DSM 3747--was optimized. Using different methods (carbodiimide, epoxy activated carriers) it was possible to immobilize the crude hydantoinase from A. aurescens DSM 3747 to supports containing primary amino groups with a yield of up to 60%. Immobilization on more hydrophobic supports such as Eupergit C and C 250 L resulted in lower yields of activity, whereas the total protein coupled remained constant. All attempts to immobilize the crude L-N-carbamoylase resulted in only low activity yields. Therefore, the enzyme was highly purified and used in immobilization experiments. The pure enzyme could easily be obtained in large amounts by cultivation of a recombinant Escherichia coli strain following a three step purification protocol consisting of cell disruption, chromatography on Streamline diethylaminoethyl and Mono Q. The immobilization of the L-N-carbamoylase was optimized with respect to the coupling yield by varying the coupling method as well as the concentrations of protein, carrier and carbodiimide. Using 60 mM of water-soluble carbodiimide, nearly 100% of the enzyme activity and protein could be immobilized to EAH Sepharose 4B.     

Cloning, nucleotide sequence and expression of a hydantoinase and carbamoylase gene from Arthrobacter aurescens DSM 3745 in Escherichia coli and comparison with the corresponding genes from Arthrobacter aurescens DSM 3747

The genes encoding hydantoinases (hyuH1) and carbamoylases (hyuC1) from Arthrobacter aurescens DSM 3745 and Arthrobacter aurescens DSM 3747 (hyuH2, hyuC2) were cloned in Escherichia coli and the nucleotide sequences determined. The hydantoinase genes comprised 1,377 base pairs and the carbamoylase genes 1,239 base pairs each. Both hydantoinases, as well as both carbamoylases, showed a high degree of nucleotide and amino acid sequence identity (96-98%). The hyuH and hyuC genes were expressed in E. coli under the control of the rhamnose promoter and the different specific activities obtained in E. coli crude extracts were compared to those produced by the original hosts. For purification the hyuH2 gene was expressed as a maltose-binding protein (MalE) and as an intein-chitin binding domain (CBD) fusion in E. coli. The expression of malE-hyuH2 resulted in the production of more soluble and active protein. With respect to temperature stability, optimal pH and optimal temperature, substrate and stereospecificity, the purified fusion enzyme exhibited properties similar to those of the wild-type enzyme.     

Cloning, nucleotide sequence and expression of a new L-N-carbamoylase gene from Arthrobacter aurescens DSM 3747 in E. coli

An L-N-carbamoyl amino acid amidohydrolase (L-N-carbamoylase) from Arthrobacter aurescens DSM 3747 was cloned in E. coli and the nucleotide sequence was determined. After expression of the gene in E. coli the enzyme was purified to homogeneity and characterized. The enzyme was shown to be strictly L-specific and exhibited the highest activity in the hydrolysis of beta-aryl substituted N alpha-carbamoyl-alanines as e.g. N-carbamoyl-tryptophan. Carbamoyl derivatives of beta-alanine and charged aliphatic amino acids were not accepted as substrates. The N-carbamoylase of A. aurescens DSM 3747 differs from all known enzymes with respect to its substrate specificity although amino acid sequence identity scores of 35-38% to other N-carbamoylases have been detected. The enzyme consists of two subunits of 44,000 Da, and has an isoelectric point of 4.3. The optima of temperature and pH were determined to be 50 degrees C and pH 8.5 respectively. At 37 degrees C the enzyme was completely stable for several days.     

Production of D-amino acids from D,L-5-substituted hydantoins by an Agrobacterium tumefaciens strain and isolation of a mutant with inducer-independent expression of hydantoin-hydrolysing activity

Conversion of D,L-p-hydroxyphenylhydantoin to D-p-hydroxyphenylglycine by Agrobacterium tumefaciens RU-OR involved a racemase, an hydantoinase and an unusual D-selective N-carbamylamino acid amidohydrolase which was active at alkaline pH and was not inhibited by N-carbamyl-L-amino acids. Enzyme activity was induced by growth in media containing 2-thiouracil. A mutant strain (RU-ORL5) was isolated, which expressed both the hydantoinase and N-carbamylamino acid amidohydrolase enzymes in the absence of inducer. © Rapid Science Ltd. 1998     

Characterization of suppressive immunoglobulin-binding factor (IBF). I. Production of IBF by a theta-positive lymphoma (L-5178-Y).

L-5178-Y, a theta-positive, Fc receptor-bearing mouse thymoma cell line spontaneously releases immunoglobulin-binding factor (IBF) upon short-term incubation in vitro. IBF produced by L-5178-Y cells is identical in its biologic activity with IBF produced by Fc receptor positive alloantigen-activated T cells. It suppresses the in vitro plaque response of mouse spleen cells to sheep erythrocytes by interfering mainly with the late phase of the generation of antibody-forming cells. Therefore, L-5178-Y thymoma affords a homogeneous source of IBF in sufficient quantities for the study of its biochemical nature and the mechanism by which it interferes with cells participating in antibody synthesis.     

Production of vanillic acid from vanillin by resting cells of Serratia marcescens

Resting-cell suspensions of Serratia marcescens were able to convert, quantitatively, 0.3% vanillin to vanillic acid. The vanillic acid-producing activity reached a maximum after 28 h of incubation with 0.01% vanillin as an inducer.     

Production and physicochemical characterization of acidocin D20079, a bacteriocin produced by Lactobacillus acidophilus DSM 20079

Lactobacillus acidophilus DSM 20079 is the producer of a novel bacteriocin termed acidocin D20079. In this paper, a partial sequence of this peptide is determined, together with data on its secondary structure. A modification of the MRS-growth medium (replacing the detergent Tween 80 with oleic acid), was shown to improve the production level of the peptide by one order of magnitude, as well as to stabilize the activity level. Addition of a detergent (Tween 20, less interfering in mass spectrometric analysis), was however necessary for solubilization of the purified acidocin D20079. Digestion of the peptide followed by de-novo sequencing of generated fragments, allowed determination of a partial sequence consisting of 39 of the totally estimated 65 residues. Acidocin D20079 has a high content of glycine residues, hydrophobic residues, and acidic residues. No modified amino acids were found. Edman degradation, and C-terminal sequencing failed, suggesting that the peptide may be cyclic, and a novel member of class IIc bacteriocins. Circular dichroism spectroscopy and secondary structure prediction showed random coil conformation in aqueous solution, but secondary structure was induced in the presence of sodium-dodecyl sulfate. The data could be fitted assuming 2–13% of the residues to be in α-helix and 23–27% of the residues to be in β-strand conformation. This indicates that a membrane/membrane-mimicking hydrocarbon–water interface induces an active conformation.     

Production and Characterization of a Polymer from Arthrobacter sp

An Arthrobacter sp. isolated from a glucose-sucrose agar plate was found to produce a neutral, extremely viscous, opalescent extracellular polymer. Growth, polymer production, and rheological properties and chemical composition of the isolated polymer were examined. The polymer was found to be substantially different from other arthrobacter polymers. Some unusual properties included irreversible loss of viscosity with high temperature and degradation of the polymer during fermentation and upon storage at 4 degrees C. Other characteristics included dependence on sucrose for polymer production, relative pH stability, increased viscosity with increased salt concentration, and pseudoplasticity. The polymer was found to be composed primarily (if not entirely) of d-fructose. The fructose content and other characteristics suggested that the polymer was a levan.     

Production of l-Methionine-enriched cells of a mutant derived from a methylotrophic yeast,Candida boidinii

l-Methionine-enriched cells production of an ethionine-resistant mutant of Candida boidinii no. 2201 was greatly improved by the control of pH and by feeding of methanol and other medium components during cultivation in a jar fermentor. Under the optimal conditions, 38.5 g (as dry weight)_of cells abd 282 mg of pool methionine (intracellular pool of free l-methionine) per l of culture broth were obtained after 11 d of cultivation.The culture conditions for production of l-methionine-enriched cells in continuous culture were investigated. With limited methanol in continuous cultivation, pool methionine productivity reached a maximum value of 1.14 mg·l⁻¹·h⁻¹ at a dilution rate of 0.05·h⁻¹. During methanol-limited growth in continuous cultivation, the pool methionine content of the mutant was about 20–35% higher than that in batch cultivation.     

The oxidation of aminoacetone by a species of Arthrobacter

1. A micro-organism similar to Arthrobacter globiformis has been isolated from sewage by elective growth on a medium containing l-threonine as sole source of carbon and nitrogen. 2. Washed cell suspensions of the organism catalyse the complete disappearance of aminoacetone from the medium and its almost complete oxidation. 3. In the presence of iodoacetate, aminoacetone disappearance is accompanied by the accumulation of methylglyoxal, about 70% of the aminoacetone removed being accounted for in this way. 4. It is suggested that the conversion of aminoacetone into methylglyoxal is catalysed by an amine oxidase.     

Production of vanillic acid from vanillin by resting cells of Serratia marcescens.

Resting-cell suspensions of Serratia marcescens were able to convert, quantitatively, 0.3% vanillin to vanillic acid. The vanillic acid-producing activity reached a maximum after 28 h of incubation with 0.01% vanillin as an inducer.     

Production of l-serine from methanol and glycine by resting cells of a methylotroph under automatically controlled conditions

Serine production from methanol and glycine was tried using frozen-thawed resting cells of a methylotroph, Protomonas extorquens NR-1 under multi-variable controlled conditions. The conditions for l-serine formation were optimized at 30°C. The production of l-serine in 0.4% CaCl₂ solution (initial pH 8.2) was the same as in 0.1 M Tris-HCl buffer (initial pH 8.3). Increasing the initial glycine concentration promoted l-serine formation. A high aeration rate decreased l-serine production. The optimum concentrations of dissolved oxygen and methanol were 0.5 ppm and 10 g/l, respectively. The highest l-serine, 24.9 g/l, was obtained at 24 h from 30.94 gl (as dry weight) resting cells using 100 g/l initial glycine with controlled pH. The relationship between the initial rate of l-serine formation and cell concentration indicated an unusual curve due to the effects of the added NaOH which was used for controlling the pH. In similar experiments without control of pH, a normal profile was observed with respect to the relationship between the initial rate of l-serine formation and cell concentration. The highest l-serine, 54.5 g/l, was obtained at 48 h by 36.4 g/l (as dry weight) resting cells. The yield (mol of l-serine/mol of added substrate) of l-serine from methanol and glycine were 8.3% and 39.3%, respectively. The selectivity of l-serine (mol of l-serine/mol of glycine consumed) was 67.9%. The stoichiometry of the maximum l-serine formation showed that the resting cells carried the highly active methanol dehydrogenase while serine transhydroxymethylase was rather low. Serine glyoxalate aminotransferase was not completely inhibited by the high concentration of glycine (about 68% of synthesized l-serine was detected in the supernatant.     

Photoactivation of pseudomonad L-tryptophan oxygenase by electron ejection from its substrate, L-tryptophan

Chemically oxidized, catalytically inactive, pseudomonad l-tryptophan-2,3-dioxygenase (EC 1.13.1.12) can be photoactivated aerobically as well as anaerobically by light of wavelength less than 360 nm. The substrate, l-tryptophan, must be present for photoactivation to proceed. In these studies, a CCl₄ filter was used to block light of wavelength less than 265 nm, preventing photolysis of water and the concomitant production of H₂O₂ (known reductant of tryptophan oxygenase). Photoactivation is not inhibited by superoxide dismutase or formate and is only slightly inhibited by catalase. Nonsubstrate analogues of l-tryptophan, 5-fluorotryptophan (binds to the catalytic site), and α-methyltryptophan (binds to the allosteric site), separately or in concert, do not mediate photoactivation, while another substrate, 6-fluorotryptophan, can. Saturation of the allosteric site with α-methyltryptophan increases the extent of photoactivation in the presence of a nonsaturating level of l-tryptophan, indicating that photoactivation is dependent on the extent of saturation of the catalytic site by l-tryptophan. During the time course of photoactivation, catalytic activity increases faster than does the formation of ferroheme enzyme, indicating that the fully reduced enzyme, (ferroheme)₂(Cu⁺)₂, is formed from the fully oxidized enzyme, (ferriheme)₂(Cu²⁺)₂, subsequent to photoactivation. A significant amount of the half-reduced, catalytically active enzyme, (ferriheme)₂(Cu⁺)₂, exists during the time course of photoactivation. We propose that the mechanism by which electrons enter tryptophan oxygenase is via “electron ejection” [T. R. Hopkins and R. Lumry (1972) Photochem. Photobiol.15, 555–566] from a photoexcited l-tryptophan bound at, the catalvtic site.     

Production of biosurfactants by the resting cells ofPseudomonas aeruginosa CFTR-6

A resting cell system was used for the production of glycolipids byPseudomonas aeruginosa CFTR-6. In this, the growth phase was separated from the production phase to overcome the inhibition of glycolipid production by inorganic phosphate. It was shown that when the cells were transferred after the growth phase into a medium devoid of phosphate, glycolipid production was increased nearly twofold. The maximum glycolipid concentration was attained much more rapidly than the conventional batch fermentation system, thus increasing the productivity.