Study of the effects of temperature, pH and yeast extract on growth and exopolysaccharides production by Propionibacterium acidi-propionici on milk microfiltrate using a response surface methodology

AIMS: To study the effects of temperature, pH and yeast extract (YE) concentration on growth and exopolysaccharide (EPS) production by Propionibacterium acidi-propionici DSM 4900 cultivated on milk microfiltrate. METHODS AND RESULTS: A multifactorial approach using a Response Surface Methodology (RSM) was followed. The results indicated that both growth, and EPS and organic acids production, were influenced by pH, temperature and YE concentration. Biomass and organic acids production occurred in all the tested domains, whereas EPS production was only possible in a narrow pH range (5.3-6.5). The results clearly showed that the optimal conditions for EPS production were different to those for optimal growth. The effect of YE on EPS production was not only due to an increase in growth but also to a direct effect on the production of EPS. The temperature played a major role. A decrease of temperature induced a slowing down of both growth and organic acids production, making the essential factors of the medium and the precursors of EPS biosynthesis more available and hence, leading to an increase in EPS production. CONCLUSION: The effects of pH, temperature and YE were determined, allowing the definition of favourable, though non-optimal, conditions for EPS production: 23 degrees C, pH 6 and 3 g l(-1) YE concentration. SIGNIFICANCE AND IMPACT OF THE STUDY: The use of a multifactorial approach for investigating the effect of fermentation conditions on EPS production has been demonstrated.     

Batch and continuous production of propionic acid from whey permeate by Propionibacterium acidi-propionici in a three-electrode amperometric culture system

Summary Growth of Propionibacterium acidi-propionici was studied on lactose as substrate and in acid whey permeate in a three-electrode poised-potential system with cobalt sepulchrate as artificial electron donor. In batch culture experiments in a stirred-tank reactor the substrate was fermented completely to propionic acid up to 6.5 g 1^–1 lactose in a supplemented whey permeate medium. No acetic acid was produced during the growth of P. acidi-propionici. An electron flow of 80–100 mA was obtained and the electron balance was 101%. In continuously growing cultures with 3 g 1^–1 of lactose as the substrate, propionate was formed as the only fermentation product up to a dilution rate (D) of 0.04 h^–1. With D>0.04 h^–1 the bacteria immobilized on the working electrode surface. It was examined whether an electron transfer occurred between the platinum working electrode and the immobilized cells. Correspondence to: W. Trösch     

Exopolysaccharide production by Bifidobacterium longum BB-79

Bifidobacterium longum BB-79 produced an acidic extracellular polysaccharide (EPS), especially when grown on solid medium. The EPS was isolated by ethanol precipitation followed by dialysis and lyophilization. Anion exchange and gel-filtration chromatography were used to further purify and characterize the EPS. The average molecular weight was greater than 200 kDa as estimated by chromatography. Based on gas-liquid chromatography (GLC) and GLC-mass spectrometry analyses, the EPS appears to be composed of galactose and an unidentified hexose (possibly glucose) with a carboxyethyl (lactic acid) substituent. Lactose, when used as the primary carbon source in liquid media, gave the highest yield of EPS. Incubation times longer than 24 h and the initial culture pH (pH 6·0–9·0) had little effect on the amount of EPS produced.     

Exopolysaccharide production by Acremonium diospyri in continuous culture

Production of an exopolysaccharide (glucan) by Acremonium diospyri was not markedly affected by its specific growth rate, the culture pH or the stirrer speed under NH ₄ ⁺ -limiting chemostat conditions. The exopolysaccharide was also detected in the medium under conditions of NH ₄ ⁺ excess.P. Wood and R.J. Seviour are with the Biotechnology Research Centre, La Trobe University College of Northern Victoria, Bendigo, Victoria 3550, Australia     

Exopolysaccharide production by free and immobilized microbial cultures

The batch production of different exopolysaccharides (alginate, xanthan, pullulan, dextran) by free and immobilized microbial cultures was investigated. First, conventional free-cell cultures were performed to obtain control fermentation parameters and macromolecular characteristics of exopolysaccharides. Then microbial cultures were immobilized in composite agar layer/microporous membrane structures and tested for polysaccharide production. The immobilized-cell system proved unsuitable for xanthan and pullulan production. Owing to the fouling of the microporous membrane by the polysaccharide, dextran production by immobilized Leuconostoc mesenteroides also was inefficient. More promising results have been obtained with immobilized Azotobacter vinelandii cultures. The amount of alginate produced by immobilized A. vinelandii represented about 60% of that recovered from a free-cell culture, whereas the polysaccharide yield reached 35% instead of 9% for the free counterpart. These results are compared to the macromolecular characteristics of exopolysaccharides.     

Fed-batch propionic acid production by Propionibacterium acidipropionici

The batch fermentations were conducted using lactose as the substrate at pH 6.5 and temperature 30°C. Average batch kinetic data was eventually used to develop an unstructured mathematical model. The kinetic parameters of the model were determined by non-linear regression technique using the batch experimental results. Parametric sensitivity analysis showed the maximum specific substrate consumption rate (r_S^max) and the maintenance energy constant (m_S) to be the most sensitive parameters. The experimental observations in batch fermentation were close to the model predictions. The batch model was extrapolated to identify nutrient feeding strategies, which were tested successfully for two different fed-batch fermentations. It demonstrated enhanced propionic acid productivity. The developed model was found suitable for the design of feeding strategies to increase propionic acid production in fed-batch mode of reactor operation.     

Exopolysaccharide production by Lactobacillus casei under controlled pH

Summary The exopolysaccharide (EPS) production and growth characteristics of Lactobacillus casei CRL 87 under pH control were studied. Maximum polymer synthesis (488 mg/l) and cell viability (2.4×10¹⁰ cfu/ml) occurred when L. casei was cultured at a constant pH of 6.0 and 30°C for 24 h. However, the optimum specific EPS production (3.9×10^-5 g EPS/g cell dry weigt) and EPS yield (4.3%) were found at a pH of 4.0.     

Exopolysaccharide and kestose production by Lactobacillus sanfranciscensis LTH2590

The effect was investigated of sucrose concentration on sucrose metabolism and on the formation of exopolysaccharide (EPS) by Lactobacillus sanfranciscensis LTH2590 in pH-controlled fermentations with sucrose concentrations ranging from 20 to 160 g liter(-1). The EPS production increased and the relative sucrose hydrolysis activity decreased by increasing the sucrose concentration in the medium. The carbon recovery decreased from 95% at a sucrose concentration of 30 g liter(-1) to 58% at a sucrose concentration of 160 g liter(-1) because of the production of an unknown metabolite by L. sanfranciscensis. This metabolite was characterized as a fructo-oligosaccharide. The oligosaccharide produced by L. sanfranciscensis was purified and characterized as a trisaccharide with a glucose/fructose ratio of 1:2. The comparison of the retention time of this oligosaccharide and that of pure oligosaccharide standards using two different chromatography methods revealed that the oligosaccharide produced by L. sanfranciscensis LTH2590 is 1-kestose. Kestose production increased concomitantly with the initial sucrose concentration in the medium.     

Exopolysaccharide production by Acremonium persicinum in stirred-tank and air-lift fermentors

Summary Exopolysaccharide production by the fungus Acremonium persicinum was affected by the culture system used. The yields achieved in shake flasks were not obtained in a stirred tank reactor, except at very low stirring speeds (100 rpm). However when grown in an air-lift fermentor, exopolysaccharide levels were similar to those found with shake flask cultures. Results suggest that both dissolved oxygen tension and shear rate may determine the ability of this organism to synthesise this exopolysaccharide. Offprint requests to: R. J. Seviour     

Propionic acid production by whole cells of Propionibacterium freudenreichii

The microbial production of propionic acid by Propionibacterium freudenreichii NCIM 2111, has been studied in this communication. Shake-flask studies were carried out to determine the optimum combination of various process parameters like stab age, inoculum age, inoculum level, medium constituents, temperature, and the initial pH for maximizing the production of propionic acid by using central composite design method. The system was found to exhibit product inhibition and hence the product inhibition kinetics was studied. A two parameter kinetic model, taking into account of the product inhibition, was proposed. Leudeking and Piret model was used to describe the production kinetics. The result from the shake-flask studies were compared with that obtained from mechanically stirred batch bioreactor and total recycle batch bioreactor.     

Exopolysaccharide production by mucoid and non-mucoid strains of Burkholderia cepacia

Thirteen strains of Burkholderia cepacia from various origins with mucoid and non-mucoid phenotypes were assayed for exopolysaccharide (EPS) production. The EPS were characterized by glycosyl composition analysis and examination of the products resulting from lithium-ethylenediamine and Smith degradations. The results showed that all strains, including the non-mucoid strains, were able to produce EPS exhibiting the same structural features, i.e. presence of one rhamnosyl, three galactosyl, one mannosyl, one glucosyl and one glucuronosyl residues, suggesting that this EPS is representative of the B. cepacia species.     

Exopolysaccharide production by Pseudomonas NCIB11264 grown in batch culture.

Fermentation studies using batch culture indicated that exopolysaccharide production by Pseudomonas NCIBI1264 in a chemically defined medium increased under conditions of nitrogen limitation and excess carbon substrate at pH values above 6. The polysaccharide was formed from a variety of carbon substrates and its composition was not affected by the nature of the carbohydrate source. Polysacharide formation did not increase in media containing small amounts of phosphate, and, as in secondary metabolite production, it started late in the exponential growth phase continuing maximally after growth had ceased. The efficiency of glucose conversion into exopolysaccharide was low. Colorimetric, viscometric, and total carbon estimation techniques are described for determining exopolysaccharide levels in cell-free culture supernatants.     

Exopolysaccharide production by Streptococcus thermophilus SY: production and preliminary characterization of the polymer

AIMS: To evaluate the effect of yeast extract (YE) concentration, temperature and pH on growth and exopolysaccharide (EPS) production in a whey-based medium by Streptococcus thermophilus SY and to characterize the partially purified EPS. METHODS AND RESULTS: Factorial experiments and empirical model building were used to optimize fermentation conditions and the chemical composition, average molecular weight (MW) and rheological properties of aqueous dispersions of the EPS were determined. Exopolysaccharide production was growth associated and was higher (152 mg l(-1)) at pH 6.4 and 36 degrees C with 4 g l(-1) YE. High performance size exclusion chromatography of the partially purified EPS showed two peaks, with a weight average MW of 2 x 10(6) and 5 x 10(4), respectively. The EPS was a heteropolysaccharide, with a glucose : galactose : rhamnose ratio of 2 : 4.5 : 1. Its water dispersions had a pseudoplastic behaviour and showed a higher viscosity of xanthan solutions. SIGNIFICANCE AND IMPACT OF THE STUDY: The fermentation conditions and some properties of an EPS produced by Strep. thermophilus, a dairy starter organism, were described.     

Exopolysaccharide production by Pseudomonas NCIB11264 grown in continuous culture.

Exopolysaccharide formation by Pseudomonas NCIB11264 in a single-stage continuous culture was maximal under nitrogen limitation with excess carbohydrate substrate at 30 +/- 1 degrees C and pH 7.0 +/- 0.1. Polysaccharide production was not enhanced by phosphate limitation but was dependent on the dilution rate. Steady states were maintained for up to 500 h without deterioration of the culture or the development of mutant strains. The efficiency of conversion of the glucose substrate utilized into exopolysaccharide by the chemostat cultures was as high as 73%.     

Exopolysaccharide production by filamentous fungi: the example of Botryosphaeria rhodina

One-hundred and five fungal strains, belonging to 46 different species, were screened for exopolysaccharide production. Phytopathogenicity and, in particular, inability to produce conidia, were physiological characteristics positively associated and correlated with the fungal ability to produce polysaccharides. Among the 29 positive strains, Botryosphaeria rhodina DABAC-P82 was the most interesting reaching, when grown on optimal nitrogen source and concentration (NaNO₃ and 2.0 g l⁻¹, respectively) and culture medium pH (3.7), 17.7 g l⁻¹ of exopolysaccharide production after only 24 h of fermentation; yield and productivity were 0.69 g g⁻¹ and 0.73 g l⁻¹ h⁻¹, respectively. The purified polysaccharide was characterised as a homopolysaccharide of glucose with a molecular weight of 4.875·10⁶ Da. Studies of structural analysis indicated the presence of β-1,3 and β-1,6 linkages; the EPS structure was very similar to that of scleroglucan. This revised version was published online in August 2006 with corrections to the Cover Date.     

Exopolysaccharide production by a unicellular cyanobacterium isolated from a hypersaline habitat

The unicellular cyanobacterial strain 16Som2, isolated from a Somaliland saltpan and identified asCyanothece sp., is characterized by cells surrounded by a thick polysaccharidic capsule, the external part of which dissolves into the medium during growth, causing a progressive increase in culture viscosity. In spite of this, the thickness of the capsule remained almost constant under all the culture conditions tested, demonstrating that the processes of its synthesis and solubilization occurred at a similar rate. The synthesis of carbohydrates was neither enhanced by increasing salinity (sea-water enriched with NaCl in the range 0 to 2.0 M) nor by Mg²⁺, K⁺ or Ca²⁺ deficiencies. In contrast, N-limitation and, to a lesser extent, P-limitation induced a significant enhancement of carbohydrate synthesis; in particular, N-deficiency stimulated the synthesis of all the carbohydrate fractions (intracellular, capsular and soluble). The soluble polysaccharide, separated from the culture medium and hydrolyzed with 2N trifluoroacetic acid, showed a sugar composition consisting of glucuronic acid: galacturonic acid: galactose: glucose: mannose: xylose: fucose in a molar ratio of 1: 2: 2.4: 6.8: 4.8: 2.9: 1.6.Cyanothece sp. culture subjected to nitrogen starvation synthesized polysaccharide with a mean productivity of 115 mg (EPS) l^–1d^–1, for the polymer solubilized into the medium, and of 15 mg (CPS) l^–1d^–1 for the capsular polysaccharide.     

Comparative studies of porphyrin production in Propionibacterium acnes and Propionibacterium granulosum.

Porphyrin production by Propionibacterium acnes and that by Propionibacterium granulosum were compared. Porphyrin synthesized by both organisms was identified as coproporphyrin III on the bases of absorption and fluorescence spectra and behavior on paper chromatography and thin-layer chromatography. Quantitative, rather than qualitative, differences in production were found between these organisms. In general, P. granulosum produced significantly greater amounts (P less than 0.001) of porphyrin than did P. acnes. delta-Aminolevulinic acid synthetase appeared to be the rate-limiting enzyme of the heme biosynthetic pathway in both organisms. The increased porphyrin production in P. granulosum is apparently associated with increased delta-aminolevulinic acid synthetase activity.     

Exopolysaccharide production on low-grade maple sap by Enterobacter agglomerans grown in small scale bioreactors

Enterobacter agglomerans isolated from a soil sample collected in the vicinity of a sugar house was grown on low-grade maple sap: When cultivated in shake flask, Ent. agglomerans produced exopolysaccharide and α-ketoglutarate. No polysaccharide and no α-ketoglutarate were produced during growth at dissolved oxygen concentrations lower than 1% saturation in a 3.5 1 bioreactor, but succinate, lactate and formate were accumulated. In order to increase polysaccharide production, various agitation systems were adapted to 7 1 bioreactors with working volumes of 41. Highest polysaccharide yield (Y_p/s= 0.70) and biomass yield (Y_x/s= 0.17) were obtained with bioreactors agitated with four-and six-bladed Rushton turbines. Accumulation of mixed organic acids during polysaccharide production indicated that both aerobic and anaerobic conditions prevailed inside the bioreactors. Maple sap concentration higher than 60 g 1⁻¹ (as sucrose equivalent) decreased both growth and exopolysaccharide production.