Role of amino acids, betaine and choline in vitamin B12 biosynthesis by strains of Propionibacterium

This paper reports the role of amino acids, betaine and choline on vitamin B₁₂ biosynthesis in Propionibacterium shermanii 566, P. shermanii and Propionibacterium arl AKU 1251. l-Glutamic acid supplemented at the 0.05% (w/v) level in whey permeate stimulated vitamin B₁₂ production in the three organisms, whereas the influence of other amino acids differed in the three strains. A uniform increase in product formation in Propionibacterium cultures with increasing doses of betaine and choline was recorded, but with variable relative effectiveness. However, no significant difference at the 0.50 and 0.75% (w/v) levels of these two compounds was observed. The addition of betaine at 0.5% (w/v) concentration was considered optimal for maximum fermentation efficiency in the cultures. An increase of 2.8–25.7% and 5.1–40.8% in vitamin B₁₂ yield as compared to the control was observed by supplementing whey permeate medium with l-glutamic acid and betaine, respectively, at their optimum values in the organisms studied.     

Influence of 5,6-dimethylbenzimidazole (DMB) on vitamin B12 biosynthesis by strains of Propionibacterium

Work on vitamin B₁₂ biosynthesis in whey permeate using 5,6-dimethylbenzimidazole (DMB) as a precursor has often been carried out, but with no reference to the stage of fermentation at which it is to be added to the fermentation medium. In the present paper we report 168 h incubation as the optimum time for vitamin B₁₂ biosynthesis and the effect of DMB addition at four phases of fermentation, on vitamin B₁₂ productivity, growth and substrate utilization by three strains of Propionibacterium. The infusion of DMB at the end of 144 h of incubation (24 h before the end of fermentation) has been found optimum for maximum metabolic efficiency of the cultures.     

Production of vitamin B12 by immobilized cells of a propionic acid bacterium

Summary The ability of immobilized cells of propionic acid bacteria to form vitamin B₁₂ has been investigated. Propionibacterium arl AKU 1251 having a considerable activity to produce the vitamin was selected as a test organism among six strains of propionic acid bacteria tested. The whole cells were entrapped with urethane prepolymers, photo-crosslinkable resin prepolymers or several other materials such as -carrageenan, agar or sodium alginate, and their vitamin B₁₂ productivity was compared. Based on the criteria of the convenience of preparation and the stability of the cell-entrapping gels, a hydrophilic urethane prepolymer, PU-9, was employed as gel material. Satisfactory vitamin B₁₂ production was obtained when 5–10 g of wet cells precultured to the late exponential growth phase were entrapped with 1 g of the prepolymer. Addition of a suitable amount of cobaltous ion and of 5,6-dimethyl benzimidazole to the culture medium was effective for the production of the vitamin by the immobilized cells. The repeated use of the immobilized cells was successfully achieved when a suitable amount of cells were entrapped and allowed the proliferation of cells inside gel matrices.     

Optimization of a Propionibacterium acidipropionici continuous culture utilizing sucrose

To produce propionic acid and vitamin B₁₂ from sucrose, the strain Propionibacterium acidipropionici NRRL B3569 was selected by screening a number of Propionibacterium strains. The nutrient composition and the fermentation conditions for this strain were optimized in continuous culture. The investigations show that within a concentration range of 30–170 g l^–1 of sucrose in the fermentation medium, no significant substrate inhibition occurred. For the production of propionic acid and vitamin B₁₂, concentrations of 1.5 mg FeSO₄·7H₂O g^–1 dry biomass, 0.75 mg cobalt ions g^–1 dry biomass, 0.3 mg 5,6-dimethylbenzimidazole g^–1 dry biomass, and 12 g yeast extract 1^–1 were necessary additions to the sources of nitrogen, phosphate, and magnesium ions. The extra addition of up to 2.8 g betaine g^–1 dry biomass significantly increases the production of vitamin B₁₂. In the optimization of the pH value, temperature, and aeration, it was established that the conditions for propionic acid production and vitamin B₁₂ production are different. Whereas the optimal production of propionic acid took place under completely anaerobic conditions with a pH value of 6.5 and a temperature of 37°C, optimal vitamin B₁₂ production required a temperature of 40°C and aerobic conditions (0.5 vvm aeration at 100 rpm) with a pH value of 6.5.     

Effect of chemical and microbial vitamin B<Subscript>12</Subscript> analogues on production of vitamin B<Subscript>12</Subscript>

Strain improvement by genetic manipulation or optimization of fermentation conditions for overproduction of vitamin B₁₂ has a drawback due to feed back inhibition. To resist the feed back inhibition by analogues of vitamin B₁₂ in Propionibacterium freudenrechii subsps. shermanii (OLP-5), we have tested with microbially separated B₁₂ analogues from three different strains. Microbial analogues were differentiated from commercially available vitamin B₁₂ by high pressure liquid chromatography and spectrophotometric method. An analogue isolated from NRRL-B-4327 was shown to increase vitamin B₁₂ concentration from 18.53 ± 0.15 to 31.67 ± 0.58 mg/l in OLP-5 strain. The presence of chemical analogue (ICH₂ Co(DH)₂ (H₂Py)₄) increased vitamin B₁₂ production from 16.13 ± 0.15 to 18.53 ± 0.15 mg/l in OLP-5. These findings revealed that addition of B₁₂ analogues in fermentation media have developed strain resistance to feed back inhibition by vitamin B₁₂.     

A novel recycle batch immobilized cell bioreactor for propionate production from whey lactose

Recycle batch fermentations using immobilized cells of Propionibacterium acidipropionici were studied for propionate production from whey permeate, de-lactose whey permeate, and acid whey. Cells were immobilized in a spirally wound fibrous sheet packed in a 0.5-L column reactor, which was connected to a 5-L stirred tank batch fermentor with recirculation. The immobilized cells bioreactor served as a breeder for these recycle batch fermentations. High fermentation rates and conversions were obtained with these whey media without nutrient supplementation. It took approximately 55 h to ferment whey permeate containing approximately 45 g/L lactose to approximately 20 g/L propionic acid. Higher propionate concentrations can be produced with various concentrated whey media containing more lactose. The highest propionic acid concentration obtained with the recycle batch reactor was 65 g/L, which is much higher than the normal maximum concentration of 35 to 45 g/L reported in the literature. The volumetric productivity ranged from 0.22 g/L . h to 0.47 g/L . h, depending on the propionate concentration and whey medium used. The corresponding specific cell productivity was 0.033 to 0.07 g/L . g cell. The productivity increased to 0.68 g/L . h when whey permeate was supplemented with 1% (w/v) yeast extract. Compared with conventional batch fermentation, the recycle batch fermentation with the immobilized cell bioreactor allows faster fermentation, produces a higher concentration of product, and can be run continually without significant downtime. The process also produced similar fermentation results with nonsterile whey media. (c) 1995 John Wiley & Sons, Inc.     

Batch production of propionic acid by immobilizedPropionibacterium sp

Whole cells ofPropionibacterium freudenreichii subsp.shermanii (two strains) were immobilized in a living state in 2 and 4% alginate gel and 2, 4 and 6% carrageenan gel. Production of propionic acid, acetic acid, and vitamin B₁₂ were examined. The best results were obtained in the fermentation with strains immobilized in 4% alginate gel when applied for the third time.     

Isolation of Cobalt-Resistant Strains of Propionic Acid Bacteria,Potent Producers of Vitamin B12

A method of adaptation to cobalt nitrate at high concentrations allowed us to isolate 46 strains of propionic acid bacteria Propionibacterium acidipropionici, resistant to excessive amounts of Co²⁺ in the medium. Studies of these strains revealed cultures that were most potent in synthesizing vitamin B₁₂. The yield of vitamin B₁₂ was increased 3 times, compared to parent strains.     

Continuous propionate production from whey permeate using a novel fibrous bed bioreactor

Continuous production of propionate from whey lactose by Propionibacterium acidipropionici immobilized in a novel fibrous bed bioreactor was studied. In conventional batch propionic acid fermentation, whey permeate without nutrient supplementation was unable to support cell growth and failed to give satisfactory fermentation results for over 7 days. However, with the fibrous bed bioreactor, a high fermentation rate and high conversion were obtained with plain whey permeate and de-lactose whey permeate. About 2% (wt/vol) propionic acid was obtained from a 4.2% lactose feed at a retention time of 35 to 45 h. The propionic acid yield was approximately 46% (wt/vol) from lactose. The optimal pH for fementation was 6.5, and lower fermentation rates and yields were obtained at lower pH values. The optimal temperature was 30 degrees C, but the temperature effect was not dramatic in the range of 25 to 35 degrees C. Addition of yeast extract and trypticase to whey permeate hastened reactor startup and increased the fermentation rate and product yields, but the addition was not required for long-term reactor performance. The improved fermentation results with the immobilized cell bioreactor can be attributed to the high cell density, approximately 50 g/L, attained in the bioreactor, Cells were immobilized by loose attachement to fiber surfaces and entrapment in the void spaces within the fibrous matrix, thus allowing constant renewal of cells. Consequently, this bioreactor was able to operate continuously for 6 months without encountering any clogging, degeneration, or contamination problems. Compared to conventional batch fermentors, the new bioreactor offers many advantages for industrial fermentation, including a more than 10-fold increase in productivity, acceptance of low-nutrient feedstocks such as whey permeate, and resistance to contamination. (c) 1994 John Wiley & Sons, Inc.     

Biosynthesis of Cobalamine,Erythromycin and Chlortetracycline by Streptomyces Species

Attempts were devoted to use Streptomyces aureofaciens and Streptomyces erythreus, the antibiotics producers as sources for the biosynthesis of cobalamine. The constituents of the fermentation medium and the strain play an important role in the biosynthesis of vitamin B₁₂. The same strain produced different amounts of antibiotic and vitamin on the two different constitutive media. The increase of the phosphorus concentration in the fermentation medium—within limits—increased the vitamin B₁₂ biosynthesis. The optimal concentration of phosphorus favourable for the synthesis of cobalamine was inhibitive for the antibiotic production. The phosphorus level in the fermentation medium plays an important role in the metabolism of carbohydrate and consequently on the biosynthesis of antibiotics. Low concentration of 5,6-dimethylbenzimidazole (cobalamine precursor) in the presence of suitable phosphorus induced the microorganism to increase its biosynthetic potentiality for the vitamin B₁₂ production.     

Calmodulin antagonists inhibit germination of Bacillus cereus T spores

M. RACINE, J. DUMONT, C.P. CHAMPAGNE AND A. MORIN. 1991. The effects of lactose, ammonium and phosphate on the production of extracellular polysaccharide from Propionibacterium acidi-propionici VM-25 were studied in whey-based media. The polysaccharide was composed of a water-soluble fraction (15% w/w), a water-insoluble fraction (27% w/w) and ca 65% (w/w) of ash. Up to 15 g/l of polysaccharide was produced during growth on partially deproteinated whey, supplemented with lactose, NH₄ Cl and KH₂ PO₄, after incubation at pH 7.0 and 25.C for 90 h. The final viscosity of the medium remained under 20 centipoises at the end of the fermentation (100–140 h). The fermentation of whey enabled a reduction of the lactose content up to 50%. The polysaccharide-containing fractions were composed of glucose, galactose, mannose, rhamnose and fucose and had M, < 5800. The polysaccharide may have applications as a low viscosity stabilizing agent.     

Fed-batch fermentation to produce oligonucleotides from Kluyveromyces marxianus grown on whey

Oligonucleotides (ON) extracted from yeasts are used as antiviral agents, immunostimulators, and flavour enhancers. Fed-batch fermentation of cheese whey by Kluyveromyces marxianus was carried out to produce high biomass yields to extract ON. K marxianus was grown for 20 h in medium containing 5% (w/v) dehydrated whey, at 30°C (pH 4.5), with agitation (350 rpm), and under aeration (1.0–2.0 vvm). After 20 h, media containing 10–15% (w/v) of dehydrated whey were added at different flow rates (180–230 ml/h). Samples were analyzed at 6–8 h intervals for cell count, lactose consumption, and ethanol production. Maximum production of biomass (28.13 g/l), yield (0.58 g/g), productivity (2.42 g/l per h), and specific growth rate (0.63 1/h) were obtained when medium containing 15% (w/v) of whey was added at 180 ml/h under 2 vvm aeration. Fed-batch fermentation converted 95% of whey lactose into biomass.     

Lactic acid production from whey permeate by immobilized Lactobacillus casei

Two matrices have been assessed for their ability to immobilize Lactobacillus casei cells for lactic acid fermentation in whey permeate medium. Agar at 2% concentration was found to be a better gel than polyacrylamide in its effectiveness to entrap the bacterial cells to carry out batch fermentation up to three repeat runs. Of the various physiological parameters studied, temperature and pH were observed to have no significant influence on the fermentation ability of the immobilized organism. A temperature range of 40–50°C and a pH range of 4.5–6.0 rather than specific values, were found to be optimum when fermentation was carried out under stationary conditions. In batch fermentation ～90% conversion of the substrate (lactose) was achieved in 48 h using immobilized cell gel cubes of 4 × 2 × 2 mm size, containing 400 mg dry bacterial cells per flask and 4.5% w/v (initial) whey lactose content as substrate. However, further increase in substrate levels tested (>4.5% w/v) did not improve the process efficiency. Supplementation of Mg²⁺ (1 mM) and agricultural by-products (mustard oil cake, 6%) in the whey permeate medium further improved the acid production ability of the immobilized cells under study.     

Effect of a corrinoid on <Emphasis Type="Italic">Methanosarcina barkeri</Emphasis> DNA synthesis

Methanosarcina barkeri is capable of synthesizing large amounts of corrinoids, compounds of the vitamin B₁₂ group, although not cobalamin. In the present work, exogenous cobalamin was demonstrated to upregulate DNA synthesis in M. barkeri cell suspensions incubated under air. The effect is similar to the one in Propionibacterium freudenreichii cells, though less pronounced. The growth of the archaeon under anaerobic conditions was shown to be suppressed by cobalamin and 5,6-dimethylbenzimidazole. The data obtained suggest the presence of a corrinoid-dependent ribonucleotide reductase in the archaeal cells which provides for deoxyribose precursors for DNA biosynthesis independently of the presence of molecular oxygen in the medium. Growth suppression under anoxic conditions by cobalamin and 5,6-dimethylbenzimidazole may be due to a decrease in the concentration of factor III, a polyfunctional corrinoid dominating in M. barkeri cells.     

Studies on whey fermentation using lactic acid bacteria L. acidophilus and L. bulgaricus

The fermentation process of acid curd whey using pure cultures of L. bulgaricus and L. acidophilus was investigated. The influence of the starter culture amount on the acidification rate in the fermentation was specified, the biological value of fermented and fermented-ammoniated curd whey was determined, and the ability of fermented whey to prevent the injurious effect of Bac. mesenthericus on the wheat bread quality was examined. Acid curd whey was fermented up to a titratable acidity of 19.8–21.6 g lactic acid/kg whey using L. acidophylus and L. bulgaricus. Mathematical equations were developed on the basis of experimental data to calculate the titratable acidity (A) as a functionof fermentation time (τ) and temperature (t). Fermentation and fermentation-ammoniation processes increase the biological value of whey (the content of the vitamins B₁, B₂, B₆, PP and the free amino acids increase). A new dry fodder BIOLAKTS was developed from fermented curd whey and was recommended for use in veterinary medicine. The fermentation-ammoniation process of curd whey was carried out by adding calculated amounts of non-protein nitrogen NH₄OH to increase the total protein equivalent and to achieve mutual proportions of protein and lactose 1:1.4, as in skimmed milk. Fermented-ammoniated curd whey was used to obtain a skimmed milk substitute. A dry flour lactic acid concentrate (FLC) was created as a mixture of high quality wheat flour and evaporated fermented whey in established ratios. As our experiments prove, it can be used as an additive in bread-making to prevent the spoiling of wheat bread by Bac. mesenthericus.     

Isolation of a novel Pseudomonas species SP2 producing vitamin B12 under aerobic condition

Vitamin B₁₂ is a complex biomolecule that acts as a cofactor for a variety of enzymes in microbial metabolism. Pseudomonas denitrificans is exclusively used as an industrial strain for the production of vitamin B₁₂ under aerobic conditions. However, only a few strains of Pseudomonas have been reported to possess the capability of producing this vitamin and they are strongly patent-protected. To improve the applicability of the vitamin B₁₂-producing microorganisms, a new isolate was obtained from municipal waste samples and characterized for its biological properties. The new isolate, designated as SP2, was identified to be a Pseudomonas species based on the sequence homology of its 16S rDNA. Pseudomonas species SP2 had essential genes for vitamin B₁₂ synthesis such as cobB and cobQ and produced a similar amount of vitamin B₁₂ (10.6 ± 0.05 μg/mL) as P. denitrificans ATCC 13867 in 24 h flask culture. SP2 grew well under aerobic condition with the maximum specific growth rate (µ _max ) of 0.91 ± 0.03/h, but showed a poor growth under micro-aerobic conditions. SP2 was resistant to antibiotics like streptomycin, carbenicillin, ampicillin, cefpodoxime, colistin, nalidixic acid and sparfloxacin. The ability of SP2 to grow faster and produce vitamin B₁₂ under aerobic conditions makes it a promising host for the production of some biochemicals requiring a coenzyme B₁₂-dependent enzyme, such as glycerol dehydratase.     

STUDIES ON CHLOROPLAST DEVELOPMENT AND REPLICATION IN EUGLENA : I. Vitamin B12 and Chloroplast Replication

When Euglena gracilis is grown under vitamin B₁₂ deficiency conditions, the amount of protein and of chlorophyll per cell increase with decrease of B₁₂ in the medium and consequently in the cell. The increase in cell protein is proportional to and precedes an increase in the number of chloroplasts per cell. This replication of the chloroplasts under deficiency conditions is not accompanied by nuclear or cell division. It is concluded that chloroplast replication in Euglena gracilis is independent of nuclear and cellular replication, at least under B₁₂ deficiency conditions. We established a graph of the growth of Euglena under different concentrations of vitamin B₁₂ added to the growth medium, which permitted us to calculate that at least 22,000 molecules of vitamin B₁₂ per cell are required to give normal growth.     

Gibberellic acid biosynthesis from whey and simulation of cultural parameters

This article examines the potential of lactose from whey permeate as a substrate for gibberellic acid production. In addition, the paper reports the derivation of mathematical models which simulate the various fermentation conditions to predict precise values. Of the five Fusarium moniliforme isolates screened for their ability to synthesize the gibberellic acid, F. moniliforme-1 proved to be the best strain (670 mg gibberellic acid/l) when fermentation was carried out at 28°C for 12 days. The product started to accumulate at the end of maximum growth phase (day 9) and continued until the curve reached a plateau (day 12). From the observed data and expected values, a temperature range of 27–30°C, pH range of 3.5–5.5 and an inoculum level of 10–12.5% (v/v) were considered optimal for attaining the highest product yield. However, nitrogen sources supplemented in whey permeate medium suppressed the ability of the culture under study to synthesize metabolite and utilize lactose.     

Selection and Study of Potent Lactose-Fermenting Yeasts

Whey-fermenting Kluyveromyces cultures were revealed among 105 yeast strains assimilating lactose. Eighteen strains from milk products, showing maximum potency, fermented galactose, sucrose, and raffinose, in addition to lactose. Many yeast strains fermented inulin. Most strains were resistant to cycloheximide and grew in medium containing glucose, NaCl, and ethanol at concentrations of up to 50, 11–12, and 10–12%, respectively (4°C). Three strains had mycocinogenic activity. After fermentation of whey with selected yeast strains at 30°C for 2–3 days, the ethanol concentration was 4–5%.