Fermented whey – an inexpensive feed source for a laboratory-scale selenium-bioremediation reactor system inoculated with Thauera selenatis

It is critical that an inexpensive electron- donor/carbon-source be found for selenium bioremedia-tion using the selenate-respiring bacterium, Thauera selenatis. Since acetate is a preferred substrate for growth of this organism, a method was developed for fermenting the lactose in whey to large amounts of acetate. Indigenous whey microorganisms fermented the whey lactose in this manner when grown in continuous culture at a very slow dilution rate (D = 0.05 h⁻¹). The successful use of the fermented whey lactose as the carbon-source/electron-donor feed for a laboratory-scale selenium-bioremediation reactor system, inoculated with T. selenatis, treating selenium-contaminated drainage water was also demonstrated. Selenium oxyanions and nitrate were reduced by 98%. Received: 30 October 1998 / Received revision: 26 January 1999 / Accepted: 5 February 1999     

A dominant selection system designed for copy-number-controlled gene integration in Hansenula polymorpha DL-1

To facilitate the selection of multiple gene integrants in Hansenula polymorpha, a rapid and copy-number-controlled selection system was developed using a vector containing a telomeric autonomous replication sequence and the bacterial aminoglycoside 3-phosphotransferase (APH) gene. Direct use of the unmodified APH gene as a dominant selectable marker resulted in the extremely slow growth of transformants and the frequent selection of spontaneous resistance. For the proper performance of the APHgene, a set of deleted glyceraldehyde-3-phosphate dehydrogenase (GAPDH) promoters of H. polymorpha were fused to the APH gene. The fusion construct with the 578-bp GAPDH promoter conferred G418 resistance sufficient to allow rapid growth of transformants, and thus facilitated the selection of transformants with up to 15 tandem copies of the vector. To increase further the integration copy number within the gene-dose-dependent range, the GAPDHpromoter was serially deleted down to the −61 nucleotide. With this weak expression cassette, the integration copy number could easily be controlled between 1 and 50. Tandemly integrated copies of plasmids near the end of the chromosome were mitotically stable over l50 generations. The dosage-dependent selection system of this study would provide a powerful tool for the development of H. polymorpha as an industrial strain to produce recombinant proteins. Received: 23 October 1998 / Received revision: 6 January 1999 / Accepted: 22 January 1999     

Characterisation of a starch-hydrolysing enzyme of Aspergillus niger

A UV-induced mutant strain of Aspergillus niger (CFTRI-1105-U9) overproduced a starch-hydrolysing enzyme with properties characteristically different from the known amylases of the fungus. The purified enzyme of 4.0 pI had an apparent molecular mass of 125 kDa and it dextrinised starch and then saccharified the dextrins. Patterns of the enzyme activity on starch, resulting in glucose at 60 °C and glucose, maltose and maltodextrins at 70 °C as primary products, suggested significant applications for the enzyme in starch-processing industries. Received: 29 October 1998 / Received revision: 11 January 1999 / Accepted: 19 January 1999     

A β-1,4-endoglucanase-encoding gene from Cellulomonas pachnodae

 A gene library of Cellulomonas pachnodae was constructed in Escherichia coli and was screened for endoglucanase activity. Five endoglucanase-positive clones were isolated that carried identical DNA fragments. The gene, designated cel6A, encoding an endoglucanase enzyme, belongs to the glycosyl hydrolase family 6 (cellulase family B). The recombinant Cel6A had a molecular mass of 53 kDa, a pH optimum of 5.5, and a temperature optimum of 50–55 °C. The recombinant endoglucanase Cel6A bound to crystalline cellulose and beech litter. Based on amino acid sequence similarity, a clear cellulose-binding domain was not distinguished. However, the regions in the Cel6A amino acid sequence at the positions 262–319 and 448–473, which did not show similarity to any of the known family-6 glycosyl hydrolases, may be involved in substrate binding. Received: 14 January 1999 / Received revision: 29 March 1999 / Accepted: 6 April 1999     

α-Amylase production in high cell density submerged cultivation of Aspergillus oryzae and A. nidulans

The effect of biomass concentration on the formation of Aspergillus oryzaeα-amylase during submerged cultivation with A. oryzae and recombinant A. nidulans strains has been investigated. It was found that the specific rate of α-amylase formation in chemostats decreased significantly with increasing biomass concentration in the range of approx. 2–12 g dry weight kg⁻¹. When using a recombinant A. nidulans strain in which the gene responsible for carbon catabolite repression of the A. oryzaeα-amylase gene (creA) was deleted, no significant decrease in the specific rate of α-amylase formation was observed. On the basis of the experimental results, it is suggested that the low value of the specific α-amylase productivity observed at high biomass concentration is caused by slow mixing of the concentrated feed solution in the viscous fermentation medium. Received: 13 January 2000 / Received revision: 30 June 2000 / Accepted: 1 July 2000     

Isolation and characterization of indene bioconversion genes from Rhodococcus strain I24

Rhodococcus strain I24 is able to convert indene into indandiol via the actions of at least two dioxygenase systems and a putative monooxygenase system. We have identified a cosmid clone from I24 genomic DNA that is able to confer the ability to convert indene to indandiol upon Rhodococcus erythropolis SQ1, a strain that normally can not convert or metabolize indene. HPLC analysis reveals that the transformed SQ1 strain produces cis-(1R,2S)-indandiol, suggesting that the cosmid clone encodes a naphthalene-type dioxygenase. DNA sequence analysis of a portion of this clone confirmed the presence of genes for the dioxygenase as well as genes encoding a dehydrogenase and putative aldolase. These genes will be useful for manipulating indene bioconversion in Rhodococcus strain I24. Received: 8 December 1998 / Received revision: 26 January 1999 / Accepted: 5 February 1999     

Production of exopolysaccharide by Pseudomonas sp. ATCC 31461 (Pseudomonas elodea ) using whey as fermentation substrate

An improved strain of Pseudomonas sp. ATCC 31461 (Pseudomonas elodea), capable of producing broth viscosities of 11 000 and 4700 mPa s (cP) when grown in enriched whey permeate and enriched sweet whey broths respectively, was isolated. The isolation was by serial transfers of the parent on lactose-rich and sweet whey broths. Maximum viscosities and biopolymer production were observed in 25% (v/v) whey concentration. In whey concentrations of 50% (v/v) or greater, residual glucose was detected in the broth and biopolymer production was low. This strain is capable of totally utilising the lactose in up to 50% (v/v) whey in 64 h. Enzyme activities suggest that the transport of lactose in P. elodea is by the permease system as opposed to the phosphotransferase system. The location of β-galactosidase is mainly intracellular. The improved strain is able to utilise lactose better than the parent and produce 1.6 times more intracellular β-galactosidase activity compared to the parent. Received: 3 May 1996 / Received revision: 8 August 1996 / Accepted: 10 August 1996     

Large-scale production of CMP-NeuAc and sialylated oligosaccharides through bacterial coupling

A large-scale production system of cytidine 5′-monophospho-N-acetylneuraminic acid (CMP-NeuAc) and sialyloligosaccharides was established by a whole-cell reaction through the combination of recombinant Escherichia coli strains and Corynebacterium ammoniagenes. For the production of CMP-NeuAc, two recombinant E. coli strains were generated that overexpressed the genes of CMP-NeuAc synthetase and CTP synthetase, respectively. C. ammoniagenes contributed to the formation of UTP from orotic acid. CMP-NeuAc was accumulated at 27 mM (17 g/l) after a 27-h reaction starting with orotic acid and N-acetylneuraminic acid. When E. coli cells that overexpressed the α-(2 → 3)-sialyltransferase gene of Neisseria gonorrhoeae were put into the CMP-NeuAc production system, 3′-sialyllactose was accumulated at 52 mM (33 g/l) after an 11-h reaction starting with orotic acid, N-acetylneuraminic acid, and lactose. Almost no oligosaccharide byproducts other than 3′-sialyllactose were observed after the reaction. The production of 3′-sialyllactose at a 5-l jar fermenter scale was almost the same as that at a beaker scale, which indicated the high potential of the 3′-sialyllactose production on an industrial scale. Received: 9 July 1999 / Received revision: 17 September 1999 / Accepted: 10 October 1999     

Construction of a flocculent brewer's yeast strain secreting Aspergillus nigerβ-galactosidase

One way of improving heterologous protein production is to use high cell density systems, one of the most attractive being the flocculating yeast production system. Also, lactose is available in large amounts as a waste product from cheese production processes. The construction of flocculent and non-flocculent brewer's yeast strains secreting β-galactosidase and growing on lactose is presented. A plasmid was constructed coding for an extracellular β-galactosidase of Aspergillus niger and having, as selective marker, the yeast CUP1 gene conferring resistance to copper. This selective marker allows for the transformation of wild-type yeasts. This work represents an important step towards the study of heterologous protein secretion by flocculent cells. Received: 13 January 2000 / Accepted: 23 January 2000     

Glucose repression of anthracycline formation in Streptomyces peucetius var. caesius

The effect of glucose on growth and anthracycline production by Streptomyces peucetius var. caesius was examined in a chemically defined medium. Glucose concentrations above 100 mM inhibited anthracycline synthesis in the original strain without causing significant change in growth and final pH values. This effect was observed when the carbohydrate was added initially or after 24 h fermentation, but not when added during the stationary growth phase. When the microorganism was pregrown in 100 mM glucose and then transferred to a resting cell system with 444 mM glucose, no significant differences in antibiotic production were observed compared to the control without glucose. The negative effect of glucose on antibiotic synthesis was not observed in a mutant (2-dog^R–21) resistant to growth inhibition by 2-deoxyglucose. Glucose consumption by this mutant was approximately 30% of that utilized by the original strain. Compared to the original strain, the mutant 2-dog^R–21 exhibited a reduction of 50% in glucose transport and an 85% decrease in glucose kinase activity. The experimental evidence obtained suggests that glucose represses anthracycline formation in a transitory manner and that this effect is related to glucose transport and phosphorylation. Received: 15 January 1999 / Received revision: 7 April 1999 / Accepted: 1 May 1999     

Molecular studies on isopenicillin N synthases

The isopenicillin N synthases isolated thus far are related to oxidases from other microorganisms and plants. These enzymes maintain a non-heme monoferrous-dependent catalytic centre comprising a HisXAsp(53–57)XHis motif and a crucial substrate-binding pocket with an ArgXSer motif for their functionality. The elucidation of these motifs was dependent on information collated from studies on structural chemistry, structural biology, site-directed engineered mutations and biochemical experiments. It is envisaged that these enzymes can potentially be improved through molecular breeding and protein engineering. Received: 15 December 1999 / Received revision: 26 January 2000 / Accepted: 27 January 2000     

Bioconversion of alpha pinene to verbenone by resting cells of Aspergillus niger

Resting cells of a locally isolated strain of Aspergillus niger caused the bioconversion of alpha pinene to verbenone. The formation of verbenone was raised from trace amounts (under screening conditions) to 3.28 mg/100 ml (equivalent to a molar yield of 16.5% conversion of the substrate) by amending the cultivation medium for the fungus. The optimal conditions were: 6 g/100 ml for the glucose concentration, a pH of 7.0, an alpha pinene concentration of 20 mg/100 ml, and a 6-h incubation period for the reaction. Received: 9 August 1999 / Received revision: 24 September 1999 / Accepted: 24 September 1999     

Production of xanthan gum and ice-nucleating material from whey by Xanthomonas campestris pv. translucens

Xanthomonas campestris pv. translucens IFO13599 could produce xanthan gum (18.5 mg/100 mg, lactose) with lactose as the growth substrate in spite of a low level of β-galactosidase. This productivity corresponded to one-fifth that with glucose. This strain could also produce ice-nucleating material having an ice-nucleating temperature, T ₅₀, of −2.8 °C with xanthan gum in the culture broth. We found that this strain produced both materials in whey medium from which the insoluble components had been removed. The production of xanthan with ice-nucleating material reached a maximum after cultivation for 168 h under optimum conditions. Furthermore, the xanthan obtained had a low viscosity because of its variant structure revealed, by TLC and HPLC analyses, to be lacking pyruvic acid. Furthermore, we concluded that this mixture had considerable potential as a regeneratic agent, when compared to other regeneratic agents such as carboxymethylcellulose. Received: 29 August 1997 / Received revision: 17 November 1997 / Accepted: 18 November 1997     

A Gram-negative bacterium producing a heat-stable nitrilase highly active on aliphatic dinitriles

A Gram-negative bacterial strain, identified as Acidovorax facilis strain 72W, has been isolated from soil by enrichment using 2-ethylsuccinonitrile as the sole nitrogen source. This strain grows on a variety of aliphatic mono- and dinitriles. Experiments using various heating regimes indicate that nitrile hydratase, amidase and nitrilase activities are present. The nitrilase is efficient at hydrolyzing aliphatic dinitriles to cyanoacid intermediates. It has a strong bias for C₃–C₆ dinitriles over mononitriles of the same chain length. Whole, resting cell hydrolysis of 2-methylglutaronitrile results in 4-cyanopentanoic acid and 2-methylglutaric acid as the major products. Heating, at least 20 min at 50 °C, eliminates nitrile hydratase and amidase activities, resulting in greater than 97% selectivity to 4-cyanopentanoic acid. The nitrilase activity has good heat stability, showing a half-life of 22.7 h at 50 °C and a temperature optimum of at least 65 °C for activity. The strain has been deposited as ATCC 55746. Received: 26 January 1999 / Received revision: 10 June 1999 / Accepted: 27 June 1999     

Pullulan production from deproteinized whey by Aureobasidium pullulans

Aureobasidium pullulans P56 was investigated using an adaptation technique and a mixed culture system. The adaptation of A. pullulans and the mixed cultures of A. pullulans and/or Lactobacillus brevisX20, Debaryomyces hansenii 194 and Aspergillus niger did not increase the production of polysaccharide. Enzymic hydrolysis of lactose in deproteinized whey gave a higher polysaccharide concentration and polysaccharide yield than acidic hydrolysed lactose. Maximum polysaccharide concentration (11.0 ± 0.5 g L⁻¹), biomass dry weight (10.5 ± 0.4 g L⁻¹), polysaccharide yield (47.2 ± 1.8%) and sugar utilization (93.2 ± 2.8%) were achieved using enzyme-hydrolysed whey (pH 6.5) containing 25 g L⁻¹ lactose and supplemented with K₂HPO₄ 0.5%, L-glutamic acid 1%, olive oil 2.5%, and Tween 80 0.5%. In this case the pullulan content of the crude polysaccharide was 40%. Received 16 December 1997/ Accepted in revised form 12 March 1999     

Mechanism of l-methionine overproduction by Escherichia coli: the replacement of Ser-54 by Asn in the MetJ protein causes the derepression of l-methionine biosynthetic enzymes

We derived l-methionine-analogue-resistant mutants from Escherichia coli JM109 strain by mutagenesis with N-methyl-N′-nitro-N-nitrosoguanidine and selected the potent l-methionine-overproducing strains by microbioassay using lactic acid bacteria. One of the mutants, strain TN1, produced approximately 910 mg l-methionine/l following the addition of 0.1% yeast extract to fundamental medium containing glucose and ammonium sulfate. The l-methionine biosynthetic enzymes, cystathionine γ-synthase and cystathionine β-lyase, of the l-methionine-overproducing mutants were little repressed by l-methionine. To analyse the mechanism of l-methionine overproduction in the mutant strains, the metJ gene coding for the E. colimet repressor, MetJ protein, was cloned and sequenced by the polymerase chain reaction. The same single-amino-acid subsitution (wild-type Ser → Asn) at position 54 was observed in four independent l-methionine-producing mutants. When the wild-type metJ gene was then introduced into strain TN1 having the mutant metJ gene, the level of enzyme synthesis and the l-methionine productivity in the transformants were found to revert to those of the wild-type. It was therefore considered that only one point mutation in the metJ gene occurred in the l-methionine-producing mutants. These results demonstrate the important role of residue 54 of the MetJ protein in l-methionine overproduction, probably because of the derepression of l-methionine biosynthetic enzymes. Received: 6 January 1999 / Received last revision: 19 February 1999 / Accepted: 26 February 1999     

Gene cloning and overproduction of low-specificity d-threonine aldolase from Alcaligenes xylosoxidans and its application for production of a key intermediate for parkinsonism drug

The dtaAX gene encoding a pyridoxal 5′-phosphate (pyridoxal-P)-dependent low-specificity d-threonine aldolase was cloned from the chromosomal DNA of Alcaligenes xylosoxidans IFO 12669. It contains an open reading frame consisting of 1,134 nucleotides corresponding to 377 amino acid residues. The predicted amino acid sequence displayed 54% identity with that of d-threonine aldolase from gram-positive bacteria Arthrobacter sp. DK-38, but showed no significant similarity with those of other known pyridoxal-P enzymes. This gram-negative bacterial enzyme was highly overproduced in recombinant Escherichia coli cells, and the specific activity of the enzyme in the cell extract was as high as 18 U/mg (purified enzyme 38.6 U/mg), which was 6,000 times higher than that from the wild-type Alcaligenes cell extract. The recombinant enzyme was thus feasibly purified to homogeneity by ammonium sulfate fractionation and DEAE-Toyopearl chromatography steps. The recombinant low-specificity d-threonine aldolase was shown to be an efficient biocatalyst for resolution of l-β-3,4-methylenedioxyphenylserine, an intermediate for production of a therapeutic drug for Parkinson's disease. Received: 9 September 1999 / Received revision: 1 November 1999 / Accepted: 12 November 1999     

Effect of temperature and pH on growth and product formation of Lactococcus lactis ssp. lactis ATCC 19435 growing on maltose

Lactococcus lactis ssp. lactis ATCC 19435 is known to produce mixed acids when grown on maltose. A change in fermentation conditions only, elevated temperatures (up to 37 °C) and reduced pH values (down to 5.0) resulted in a shift towards homolactic product formation. This was accompanied by decreased growth rate and cell yield. The results are discussed in terms of redox balance and maintenance, and the regulation of lactate dehydrogenase and pyruvate formate-lyase. Received: 14 December 1998 / Received revision: 12 January 1999 / Accepted: 22 January 1999     

A novel method for characterisation of microbial growth kinetics on volatile organic compounds

A novel method for the determination of microbial growth kinetics on hydrophobic volatile organic compounds (VOC) has been developed. A stirred tank reactor was operated as a fed-batch system to which the VOC was continuously fed via the gas phase, assuring a constant VOC concentration in the mineral medium. A flow of air was saturated with the VOC, and then mixed with a further flow of air, to obtain a predetermined VOC concentration. Thus, different VOC concentrations in the mineral medium could be obtained by altering the VOC concentration in the feed gas. The growth kinetics of Xanthobacter autotrophicus GJ10 on 1,2-dichloroethane (DCE) and of Pseudomonas sp. strain JS150 on MonoChloroBenzene (MCB) were assessed using this method. The growth of strain JS150 was strongly inhibited at MCB concentrations higher than 160 mg l⁻¹, and the results were fitted using a piecewise function. The growth kinetics of strain GJ10 were described by the Luong model where maximum growth rate μ_max = 0.12 h⁻¹, substrate saturation constant K _S = 7.8 mg l⁻¹, and maximum substrate concentration S _m (above which growth is completely inhibited) = 1080 mg l⁻¹. Varying nitrogen and oxygen flows enabled the effect of oxygen concentration on the growth kinetics of Pseudomonas JS150 to be determined. Received: 30 November 1998 / Received revision: 19 March 1999 / Accepted: 20 March 1999     

Metabolic responses to different glucose and glutamine levels in baby hamster kidney cell culture

In this work, a BHK21 clone producing a recombinant antibody/cytokine fusion protein was used to study the dependence of cell metabolism on the glucose and glutamine levels in the culture medium. Results obtained indicate that both glucose and glutamine consumptions show a Michaelis-Menten dependence on glucose and glutamine concentrations respectively. A similar dependence is also observed for lactate and ammonia productions. The estimated value of the Michaelis constant for the dependence of lactate production on glucose (K ^Glc _Lac) was 1.4 ± 0.1 mM and for the dependence of ammonia production on glutamine (K ^Gln _Amm) was 0.25 ± 0.11 mM and 0.10 ± 0.03 mM, at glucose concentrations of 0.28 mM and 5.6 mM respectively. At very low glucose concentrations, the glucose to lactate yield decreased markedly, showing a metabolic shift towards lower lactate production. This␣metabolic shift was also confirmed by the significant increase in the specific oxygen consumption rate also observed at low glucose concentrations. Although it was␣highly dependent on glucose concentration, the oxygen consumption also increased with the increase in␣glutamine concentration. At very low glutamine concentrations, the glutamine to ammonia yield increased, showing a more efficient glutamine metabolism. Received: 21 August 1998 / Received revision: 11 November 1998 / Accepted: 17 January 1999