Synthesis of Several 3,4-Methylenedioxyphenyl Derivatives as Inhibitors for Metamorphosis of Silkworm Larvae

The present purpose is to improve tartaric acid productivity of Gluconobacter suboxydans IAM 1829, which is well known as a 5-ketogluconic acid producer, by mutation involving the use of newly developed isolation method. In the course of studies for recognizing the causes suppressing the yield of tartaric acid, it was revealed that hydrogen-ion concentration and glycolic acid accumulated during fermentation limited the tartaric acid formation by inhibiting the growth of the bacteria. From these point of view, isolation of acid tolerant mutants and glycolate tolerant mutants was carried out. The significant correlation was found between the tartaric acid productivity of these mutants and their tolerance to those inhivitory agents, and some desireable mutants were obtained.     

Cloning of a gluconate/polyol dehydrogenase gene from <Emphasis Type="Italic">Gluconobacter suboxydans</Emphasis> IFO 12528, characterisation of the enzyme and its use for the production of 5-ketogluconate in a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> strain

A 5-ketogluconate (5-KGA)-forming membrane quinoprotein, gluconate dehydrogenase, was isolated from Gluconobacter suboxydans strain IFO 12528 and partially sequenced. Partial sequences of five internal tryptic peptides were elucidated by mass spectrometry and used to isolate the two adjacent genes encoding the enzyme (EBI accession no. AJ577472). These genes share close homology with sorbitol dehydrogenase from another strain of G. suboxydans (IFO 3255). Substrate specificity of gluconate 5-dehydrogenase (GA 5-DH) turned out to be quite broad, covering many polyols, amino derivatives of carbohydrates, and simple secondary alcohols. There is a broad correlation between the substrate specificity of GA 5-DH and the empirical Bertrand-Hudson rule that predicts the specificity of oxidation of polyols by acetic acid bacteria. Escherichia coli transformed with the genes encoding gluconate dehydrogenase were able to convert gluconic acid into 5-KGA at 75% yield. Furthermore, it was found that 5-KGA can be converted into tartaric acid semialdehyde by a transketolase. These results provide a basis for designing a direct fermentation-based process for conversion of glucose into tartaric acid.     

Accumulation of Nucleic Acid-related Substances by Microorganisms

The induction of adenosine-producing mutants from an inosine-producing mutant previously derived from a Bacillus strain was attempted, and it was found out that the xanthine-requiring mutants lacking of adenase produce a large amount of adenosine.

The outline of the processes for the derivation of these mutants was described. Main product of these mutants was adenosine, and the culture broth contained a little amount of adenine as a by-product.

The culture conditions optimal for the production of adenosine were investigated, and the yield of adenosine in the culture broth was more than 16 mg/ml.     

Production of l-DOPA by Mutants of Pseudomonas melanogenum

Several kinds of mutants of Pseudomonas melanogenum were derived by mutational treatment with N-methyl-N’-nitro-N-nitrosoguanidine, and selected for 3,4-dihydroxyphenyl-l-alanine (l-DOPA) production by newly devised screening method which was carried out on agar plates based on violet-black colour formation by the reaction of l-DOPA with iron ion. Mutants tested were; glucose-insensitive mutant, cysteine-insensitive mutant, 3-amino-tyrosine-resistant mutant and p-fluorophenylalanine-resistant mutant. Some colonies isolated by monocolony procedure without mutagenic treatment were also tested. Among the 3-aminotyrosine-resistant mutants many good l-DOPA producers were found.

An 3-aminotyrosine-resistant mutant, strain ATN–36, produced 14 to 15 mg/ml of l-DOPA from 26 mg/ml of l-tyrosine (68 % in molar conversion ratio). When the cell concentration in reaction mixture was increased to 4-times the concentration of culture broth, l-DOPA production reached to 21 mg/ml from 52 mg/ml of tyrosine. An enzymatic basis of the high l-DOPA productivity of the improved mutants was found to be due to the increased tyrosinase activity (150 to 160% of the parental strain) of the mutants.     

Induction and Citric Acid Productivity of Fluoroacetate-sensitive Mutant Strains of Candida lipolytica

To establish a novel process for the economical production of citric acid from n-paraffins by yeast, attempts were made to obtain some mutant strains capable of producing citric acid in higher yield without (+)-isocitric acid.

From among the mutant strains derived from Candida lipolytica ATCC 20114, which produced citric acid and (+)-isocitric acid in the ratio of about 60:40 from n-paraffins, a citrate non-utilizing mutant strain, K-20, and a fluoroacetate-sensitive mutant strain , S-22, were selected on the basis of high citric acid and low (+)-isocitric acid productivity.

The mutant strain S-22 showed extremely poor growth in a medium containing sodium citrate as the sole carbon source and extremely high sensitivity to fluoroacetate. The production ratio of citric acid and (+)-isocitric acid by the mutant strain was changed to 97:3, and the yield of the citric acid from n-paraffins, charged to the fermentation medium, reached 145%(w/w).     

Fermentation of 1,3-propanediol by a lactate deficient mutant of Klebsiella oxytoca under microaerobic conditions

Klebsiella oxytoca M5al is an excellent 1,3-propanediol (1,3-PD) producer, but too much lactic acid yielded greatly lessened the fermentation efficiency for 1,3-PD. To counteract the disadvantage, four lactate deficient mutants were obtained by knocking out the ldhA gene of lactate dehydrogenase (LDH) of K. oxytoca M5al. The LDH activities of the four mutants were from 3.85 to 6.92% of the parental strain. The fed-batch fermentation of 1,3-PD by mutant LDH3, whose LDH activity is the lowest, was studied. The results showed that higher 1,3-PD concentration, productivity, and molar conversion rate from glycerol to 1,3-PD can be gained than those of the wild type strain and no lactic acid is produced under both anaerobic and microaerobic conditions. Sucrose fed during the fermentation increased the conversion and sucrose added at the beginning increased the productivity. In fed-batch fermentation with sucrose as cosubstrate under microaerobic conditions, the 1,3-PD concentration, conversion, and productivity were improved significantly to 83.56 g l⁻¹, 0.62 mol mol⁻¹, and 1.61 g l⁻¹ h⁻¹, respectively. Furthermore, 60.11 g l⁻¹ 2,3-butanediol was also formed as major byproduct in the broth.     

Improved Extraction of Rice Prolamin

A considerable amount of menaquinone (MK)-4 was found in cells of a l-hydroxy-2- naphthoate-resistant mutant, strain HNA 250–15, which was derived from Flavobacterium sp. 238- 7, in which MK-6 is the major isoprenoid quinone. The MK-4 productivity was further improved by making the mutant resistant to usnic acid and menadione. The amount of MK produced by the resultant mutant, strain K₃–15, produced 125.4mg/1 of culture broth and 12.8 mg/g of dry cell weight, in the ratio of MK-4 and MK-6 of 6:1, under the optimal culture conditions in the presence of cedar wood oil.     

Optimization of erythritol production by Candida magnoliae in fed-batch culture

A two-stage fed-batch process was designed to enhance erythritol productivity by the mutant strain of Candida magnoliae. The first stage (or growth stage) was performed in the fed-batch mode where the growth medium was fed when the pH of the culture broth dropped below 4.5. The second stage (or production stage) was started with addition of glucose powder into the culture broth when the cell mass reached about 75 g dry cell weight l⁻¹. When the initial glucose concentration was adjusted to 400 g l⁻¹ in the production stage, 2.8 g l⁻¹ h⁻¹ of overall erythritol productivity and 41% of erythritol conversion yield were achieved, which represented a fivefold increase in erythritol productivity compared with the simple batch fermentation process. A high glucose concentration in the production phase resulted in formation of organic acids including citrate and butyrate. An increase in dissolved oxygen level caused formation of gluconic acid instead of citric acid. Journal of Industrial Microbiology & Biotechnology (2000) 25, 100–103. Received 25 February 2000/ Accepted in revised form 08 June 2000     

Production of l-Glutamic Acid from Hydrocarbon by Penicillin-resistant Mutants of Corynebacterium hydrocarboclastus

Penicillin-resistant mutants were derived from Corynebacterium hydrocarboclastus R-7. One of them produced 84 g/liter of l-glutamic acid from hydrocarbon, though its parent strain produced 26 g/liter.

The penicillin-resistant mutant had stronger activities of substrate consumption and oxygen absorption than the parent strain, and this was one of the reasons for the accumulation of a larger quantity of l-glutamic acid.

The interacellular content of phosphatidyl inositol mannoside (P.I.M) was related to the glutamate productivity, and the higher glutamate productivity of the penicillin-resistant mutant was supposed to be related to the remarkable diminution in the content of P.I.M.     

Excretion of l-Tryptophan by Analogue-resistant Mutants of Pseudomonas hydrogenothermophila TH-1 in Autotrophic Cultures

Cells of a thermophilic hydrogen bacterium, Pseudomonas hydrogenothermophila TH-1 were treated with N-methyl-N′-nitro-N-nitrosoguanidine and resulting mutants resistant to tryptophan analogues were selected under autotrophic culture conditions (energy source, H₂; carbon source, CO₂). A mutant strain, 7922, which was resistant to 2000 µg/ml of 5-methyltryptophan and 200–500 µg/ml of 5-fluorotryptophan, was obtained by two step mutations. This mutant excreted 38–70 µg/ml of tryptophan into flask culture broth and a maximum of 200 µg/ml into jar fermentor broth.     

Bioassay of Mildiomycin and a Rapid, Cost-Effective Agar Plug Method for Screening High-yielding Mutants of Mildiomycin

Summary A simple, reliable and low-cost agar diffusion bioassay for quantitative determination of mildiomycin was developed using a strain of Rhodotorula rubra AS 2.166 as the indicator organism and potato dextrose agar at pH 7.0 as the test medium. With equivalent precision and accuracy to HPLC analysis, this method was applied to analyse mildiomycin in complex culture broth during the fermentation process. A modified agar plug method based on the bioassay was constructed for rapid and efficient screening of high-yielding mutants of mildiomycin. Within four weeks, a high production strain, the mildiomycin productivity of which was 75.5% higher than the parent strain, was obtained from 15,000 mutants.     

Decolorization of dye and molasses by continuous and semi-continuous jar-fermentor cultures ofGeotrichum candidum Dec 1

Two culture modes, continuous and semi-continuous, of the decolorization fungus,Geotrichum candidum Dec 1, were compared to obtain a high treatment efficiency of molasses decolorization and a large productivity of peroxidase (DyP) to simultaneously decolorize dyes and molasses. The continuous culture ofG. candidum Dec 1 using a 5-l jar-fermentor showed high DyP activity at a low dilution ratio of 0.005h⁻¹, and decolorization ratio of molasses of 80% was obtained concomitantly. Therefore, a semi-continuous culture was performed by repeated refill and draw. In this mode, approximately 1.5 liters of the culture broth was replaced per cycle when the decolorization ratio of molasses was near 80%. The molasses medium (1.0 liter per day) was treated and the peroxidase productivity in the drawn culture broth was 26.6 U/day, whereas the peroxidase productivity was 17.9 U/day in the continuous culture with a dilution rate of 0.005 h⁻¹. The semi-continuous treatment system was an efficient decolorization method for the strain,G. candidum Dec 1.     

Isolation of transposon Tn5 mutant affected in the metabolism of 18β-glycyrrhetinic acid

Transposon Tn5 mutagenesis was carried out to clarify the metabolism of 18-glycyrrhetinic acid (18-GRA) in Sphingomonas paucimobilis G5. A Tn5-induced mutant strain, named TM9638 that was affected in its metabolism of 18-GRA, was isolated. This mutant accumulated three metabolites, designated as M-A, M-B and M-C, from 18-GRA in the culture broth. M-A was accumulated in the culture broth of wild type strain, but M-B and M-C were not accumulated in the culture broth of wild type strain. M-B and M-C were isolated from the culture broth of TM9638 and the chemical structures were elucidated by NMR and GC-MS.     

Mutagenic Activity of Autoxidized Linolenic and Linoleic Acid

Isolation of mutants with an enhanced productivity of 7β-(4-carboxybutanamido)-cephalosporanic acid acylase (penicillin amidohydrolase, EC 3.5.1.11) was attempted. A mutant, Ci-36, isolated by a method using glutarylamlide, produced approximately 5-times more acylase than did the parental strain. However, this acylase formation was still dependent on glutaric acid which was previously found to be essential in the case of the wild strain, Pseudomonas SY-77-1. The inducible-acylase formation was found to be firmly associated with the process of cell multiplication. Subsequently, a mutant, GK-16 was derived from Ci-36, which was shown to produce the acylase at maximum level without the addition of glutaric acid. The productivity of GK-16 was 2.4-times higher than that of Ci-36.     

L-Serine Production by Temperature-sensitive Mutants of Methanol-utilizing Bacterium Pseudomonas MS 31

Temperature-sensitive mutants producing L-serine efficiently from glycine were obtained from the facultative methylotroph Pseudomonas MS 31. Forty-five mutant strains showed adequate growth on methanol at 30°C but little or no growth at 37°C. Fourteen of these mutants produced L- serine more efficiently than the wild-type strain. The typical mutant strain ts 162 showed a high conversion rate in glycine-to-L-serine when the cultivation temperature was changed from a permissive (30°C) to non-permissive state (38?42°C) together with the addition of glycine and methanol after adequate growth. The mutant strain accumulated 6.8 mg L-serine from 12 mg glycine per ml culture under optimum conditions. The reduction of L-serine degrading activity in the mutant strain seemed to contribute to the high productivity of L-serine.     

Effect of a Microbial Acid Protease Inhibitor (S-PI) on the Production of Fungal Acid Protease

Cladosporium sp. No. 45–2, an acid protease-producing microorganism, was cultured in medium containing a microbial acid protease inhibitor (S–PI). By the addition of S–PI, the amount of acid protease in the culture broth showed an increase of 50~80% over those of normal culture (S–PI-free). Acid protease was purified from the S–PI-added culture filtrate, and its enzymatic and physicochemical properties were compared with those of acid protease obtained from normal culture. It was determined that the acid protease obtained from S–PI-added culture was the same as that of normal culture, but that the productivity was increased by the addition of S–PI.

The increase in acid protease productivity is assumed to be due to a change in metabolism by the addition of S–PI.     

Tryptophan Production by a Lipoic Acid Auxotroph of Enterobacter aerogenes Having Both Pyruvic Acid Productivity and High Tryptophanase Activity

A new process for tryptophan production was established using a lipoic acid auxotrophic mutant, Enterobacter aerogenes l-12, which has both pyruvic acid productivity and tryptophanase activity. The process consists of the production of pyruvic acid from glucose by the washed cells and the subsequent conversion of the acid to tryptophan by the tryptophanase itself in the presence of indole and NH₄C1.

To prepare washed cells of which the tryptophanase activity and the pyruvic acid productivity were both high, it was best to culture the strain in a medium containing 1 % Polypepton, 0.2 % glucose, 3 μg/1 dl-lipoic acid, 0.05 % l-tryptophan, and mineral salts. The optimum composition of the reaction mixture for the pyruvic acid production by the washed cells was established. Under these conditions, 17 g/1 of pyruvic acid was accumulated from 5 % glucose after 36 hr of incubation. Thus, the conversion of the pyruvic acid to tryptophan was done by adding indole, NH₄C1, pyridoxal-5′-phosphate, Triton X-100, and KOH to adjust the pH to 9.0 to the above reaction mixture. As a result, the pyruvic acid was rapidly converted to tryptophan, and the concentration of 14 g/1 was obtained after 36 hr (total 72 hr).     

Studies on Production of Biotin by Microorganisms

The utilization of hydrocarbons by microorganisms was studied in many fields, but the production of biotin vitamers by hydrocarbon-utilizing bacteria has never been reported.

We have screened many hydrocarbon-utilizing bacteria which produce biotin vitamers in the culture broth. The effects of cultural conditions on biotin vitamers production by strain 5–2, tentatively assigned to the genus Pseudomonas, were studied.

More than 98% of biotin vitamers produced from hydrocarbons by strain 5–2 was chromatographically determined as desthiobiotin. As nitrogen source, natural nutrients were more effective than inorganic nitrogen sources. The production of biotin vitamers was increased under the condition of good aeration. Exogenous pimelic or azelaic acid enhanced biotin vitamers production by strain 5–2.

The production of biotin vitamers from n-alkanes, n-alkenes or glucose by an isolated bacterium, strain 5-2, tentatively assigned to the genus Pseudomonas, was investigated. Among these carbon sources, n-undecane was the most excellent for biotin vitamers production.

The biosynthetic pathway of biotin vitamers, especially desthiobiotin, from n-undecane was also studied. It was found by thin-layer and gas-liquid chromatographical methods that pimelic and azelaic acids were the main acid components in n-undecane culture.

This result, together with previously reported enhancement of biotin vitamers production by these acids, suggests that pimelic and azelaic acids may be the intermediates of biotin vitamers biosynthesis from n-undecane.     

Production of Nucleic Acid-Related Substances by Fermentative Processes

An adenine-requiring mutant (KY7208) of Brevibacterium ammoniagenes ATTC 6872 was found to accumulate an appreciable quantity of IMP and hypoxanthine in the culture liquid.

Crystalline IMP was isolated from culture broth of KY7208 by the use of ion-exchange columns. The preparation obtained was definitely identified as 5′-IMP, based on the results on paperchromatography, UV and IR absorption spectra, and analyses of its hydrolysates.

Growth responses of this mutant were demonstrated to adenine and adenosine, but not to 5′-AMP, 3′-AMP and 5′-AMP.

Over 5 mg of IMP per ml of broth were produced by the organism in natural medium consisting of glucose, yeast extract, urea, high concentrations of phosphate and magnesim salts, and others. The chemical changes showed that hypoxanthine first accumulated in the earlier stage of fermentation, and IMP synthesis then took place with the disappearance of hypoxanthine in the later stage of fermentation.