Production ofLactococcus lactis biomass by immobilized cell technology

Summary Calcium alginate beads containingLactococcus lactis cells were used for three batch fermentations of milk or a commercially available growth medium (Gold Complete, Nordica) with the aim of producing concentrated cultures. Repeated fermentations did not significantly increase bead CFU counts which were between 3.3–7.8×10¹⁰ CFU/g. During the second and third fermentations, which lasted 6 h each, the bead populations decreased if the incubation was extended over 2 h. There was cell release from the beads. Fermentation media and fermentation time all had an effect on free cell counts, but none of these factors statistically interacted. Free cell counts were higher at the end of fermentations 2 and 3 than in the first fermentation and approximately 50% of the population was in the free state. Free cell counts were higher when the beads were incubated in Gold complete than in milk. Although the total bacterial population of a standard free cell fermentation was always higher than those having immobilized cells, immobilized cell technology did enable the production of dense cultures.     

Studies on batch production of bacterial concentrates from mixed species lactic starters

Optimum growth conditions for mixed species starter FDs 0172 at constant pH in skim milk, whey, and tryptone medium were investigated. Growth rate and maximum population were optimal at 30 C. pH values between 5.5 and 7.0 did not influence the growth rate and maximum population obtainable. Lactic acid-producing activity declined rapidly after reaching the end of the exponential growth phase. The bacterial balance was found to be influenced by the growth parameters: media, pH, temperature, and neutralizer. Skim milk or whey medium at 25 C, pH 6.5, and neutralized with 20% (vol/vol) NH₄OH kept the bacterial balance almost constant throughout the cultivation. Grown in tryptone medium at constant pH, the changes in bacterial balance and other metabolic activities were striking compared to the other two media tested. The effect of lactate as an inhibitor was found to be complex, changing with the growth conditions. Concentrates made from mixed species starters FDs 0172, FD 0570, CH 0170, CHs 0170, and T 27 were comparable to controls when cultivated at the optimum conditions found and thereafter centrifuged. Aroma production, proteolytic activity, and CO₂ production did not change significantly compared to controls when cultivated at optimum conditions in skim milk or whey medium.     

Growth of a Mixed Species Lactic Starter in a Continuous "pH-Stat" Fermentor

Optimum growth conditions for mixed species starter FDs 0172 in skim milk, whey medium, and tryptone medium at 25 C in a “pH-stat” continuous fermentor were investigated. Specific growth rate and productivity were found to be influenced both by the medium and the pH value. Highest productivity was found in skim milk medium between pH 5.5 and 5.9. Lactic acid-producing activity of harvested cells decreased by continuous cultivation at pH values lower than 5.9 to 6.1, especially in tryptone and whey medium. Bacterial balance, CO₂ production, and aroma formation were comparable to the control in skim milk and whey medium at any pH, but differed significantly for cells grown in tryptone medium.     

Casein as a necessary factor in the production of stimulatory material for associative growth of lactic streptococci

Strains of Streptococcus cremoris KH and HC produced material that was stimulatory for S. cremoris R₆ in milk and in the dialyzable fraction of milk, but not in the dialysate fraction of milk, lactic acid whey, or lactose broth. The addition of casein to these latter media permitted the production of this stimulatory material to occur. Tryptone, peptone, and yeast extract could not be substituted for casein in producing the stimulatory material or in initiating associative growth in the lactic acid whey. The minimum concentration of casein required appeared to be from 2.0 to 2.5%.     

Improved medium for lactic streptococci and their bacteriophages

Incorporation of 1.9% β-disodium glycerophosphate (GP) into a complex medium resulted in improved growth by lactic streptococci at 30 C. The medium, called M17, contained: Phytone peptone, 5.0 g; polypeptone, 5.0 g; yeast extract, 2.5 g; beef extract, 5.0 g; lactose, 5.0 g; ascorbic acid, 0.5 g; GP, 19.0 g; 1.0 M MgSO₄·7H₂O, 1.0 ml; and glass-distilled water, 1,000 ml. Based on absorbance readings and total counts, all strains of Streptococcus cremoris, S. diacetilactis, and S. lactis grew better in M17 medium than in a similar medium lacking GP or in lactic broth. Enhanced growth was probably due to the increased buffering capacity of the medium, since pH values below 5.70 were not reached after 24 h of growth at 30 C by S. lactis or S. cremoris strains. The medium also proved useful for isolation of bacterial mutants lacking the ability to ferment lactose; such mutants formed minute colonies on M17 agar plates, whereas wild-type cells formed colonies 3 to 4 mm in diameter. Incorporation of sterile GP into skim milk at 1.9% final concentration resulted in enhanced acid-producing activity by lactic streptococci when cells were inoculated from GP milk into skim milk not containing GP. M17 medium also proved superior to other media in demonstrating and distinguishing between lactic streptococcal bacteriophages. Plaques larger than 6 mm in diameter developed with some phage-host combinations, and turbid plaques, indicative of lysogeny, were also easily demonstrated for some systems.     

Alginate-based solid media for plant tissue culture

Summary A new method for solid medium plant tissue culture based on in situ gelation of alginate is proposed as an alternative to agar-based media. In situ gelation by the use of dispersed CaCO₃ and the slowly hydrolysing acid glucono--lactone (GDL) was the basis for the use of alginate as a gelling agent. Inexpensive alginate-based media can be made in a wide range of pH values. Biological tests of these gels, concerning sterile seed growth and microcalli plating of Brassica napus (cv. Topas) and biomass production of Panax ginseng callus, showed results equal to those achieved with agar-based gels.     

Effect of medium on growth and subsequent survival,after freeze-drying,ofLactobacillus delbrueckii subsp.bulgaricus

Summary Growth ofLactobacillus delbrueckii subsp.bulgaricus, grown at a constant pH (5.7) in papain-or pepsin-treated whey was superior to that in whey or whey permeate, but inferior to growth in milk; it was not significantly different from that found in a 1:1 whey: milk medium. When 2% sodium citrate was added to the fermented medium, the cell recovery levels (59–75%) upon centrifugation were not significantly different in papain-treated media compared to untreated substrates. Cultures obtained from papain-treated milk or whey showed similar mortality levels following freeze-drying (99%) to those grown on untreated milk or whey. Addition of Tween 80 to the growth medium improved survival rate by a factor of ten.     

Selection of Protease-Positive and Protease-Negative Variants of Streptococcus cremoris

Protease-negative variants were shown to outcompete the wild-type strains of Streptococcus cremoris E₈, HP, and Wg₂ at pH values higher than 6.0 in milk. For S. cremoris E₈ this process was studied in more detail. At lower pH values the wild type had a selective advantage. This pH-dependent selection was not found in all media tested. The poor growth of the protease-negative variant at low pH was not due to lower internal pH values. By growing S. cremoris E₈ and Wg₂ in acidified milk (pH 5.9) the proteolytic activity of the cultures could be stabilized. In continuous cultures under amino acid limitation the wild type S. cremoris E₈ and HP strains had a selective advantage over the protease-negative variants at low dilution rates (D < 0.2) at all pH values of the medium. This was apparently due to a lower affinity-constant (K_s) of the protease-positive variants for amino acids. Finally, a high fraction of protease-positive variants could be maintained in continuous cultures by using a growth medium with low concentrations of casein as a nitrogen source. At high dilution rates nearly all cells were protease positive.     

Influence of Whey Protein Concentrate on the Production of Antibacterial Peptides Derived from Fermented Milk by Lactic Acid Bacteria

In the study, growth, proteolysis and antimicrobial activity of lactic acid bacteria were evaluated in skim milk medium supplemented with different concentration of whey protein concentrate (WPC 70). Lactobacillus helveticus (V3) showed maximum pH reduction with 1% WPC. Lactobacillus rhamnosus (NS4) also produced maximum lactic acid production and viable cells counts at 1 and 1.5% WPC, respectively. However, V3 showed maximum proteolytic activity with 1.5% WPC. Streptococcus thermophilus (MD2) was found to exhibit maximum antimicrobial activity with 1.5% WPC. Peptides formed during fermentation were purified by RP-HPLC and identified using RP-LC/MS analysis. Antimicrobial peptide was identified as lactoferrin, which was found in fermented milk supplemented with 1.5% WPC by NS4.     

Importance of B4 Medium in Determining Organomineralization Potential of Bacterial Environmental Isolates

B4 precipitation medium has been used as the preferred medium for studying mineral precipitation using bacterial strains in vitro since pioneer studies were performed by Boquet and coworkers in 1973. Using this medium, several authors have demonstrated that some environmental isolates were able to precipitate minerals, yet others did not. The main goal of the current study is to understand whether pH and buffer conditions would have a significant effect on mineral precipitation results for environmental isolates grown on B4. For this study, a total of 49 strains isolated from natural environments from Puerto Rico were grown on B4 plates, and their CaCO₃ precipitation potential was investigated. Our findings revealed a strong correlation between a lack of CaCO₃ precipitation and the acidification of the B4 plates by the colonies. The ability to precipitate CaCO₃ could be restored by buffering the B4 medium to a pH of 8.2. Buffering capacity of the medium was proposed to be involved in CaCO₃ precipitation: acid-base titrations conducted on the individual ingredients of B4 showed that yeast extract has a poor buffering capacity between pH 6.5–7.5. This pH range corresponds to the pH of B4 plates [6.87 (±0.05)] prior to the inoculation. This might explain why B4 is such a good precipitation medium: a small variation in the H⁺/OH^? balance during microbial growth and precipitation produces rapid changes in the pH of the medium. Finally, an amorphous matrix was distributed within 90% of the examined crystals generated on B4 medium by the environmental strains. Supplemental materials are available for this article. Go to the publisher's online edition of Geomicrobiology Journal to view the free supplemental file.     

Development of coencapsulating technology for the production of chitosanoligosaccharides

To easily separate chitosanoligosaccharides by size exclusion, an coencapsulating technology of substrate and enzyme was developed. The membrane was composed of alginate and a divalent cation such as calcium. Chitosan and chitosanase were enveloped in this membrane and the product released to medium by size exclusion. The capsule was stabilized in a 2% acetic acid solution (pH 5.0) containing 0.145 M CaCO₃. The leakage of substrate caused by the agitation speed was controlled by increasing alginate and CaCO₃ concentrations. The lower limit of the alginate concentration and the agitation speed were 0.5% and 40 rpm, respectively. Membrane thickness and capsule diameter were 10 μm and 2.5 mm, respectively. By TLC analysis, the composition of chitosanoligosaccharides were mainly 3–6 mers. The molecular weight distribution of the released oligosaccharides ranged from 262 to 3624 Da by GPC.     

Organic Acid Production by Basidiomycetes: I. Screening of Acid-Producing Strains

Sixty-seven strains belonging to 47 species of Basidiomycetes were examined for their acid-producing abilities in glucose media, in both the presence and absence of CaCO₃, in stationary and shake cultures. Some strains were found to produce large quantities of oxalic acid. The oxalic acid-producing strains could be separated into two groups. Strains of one group (mostly brown-rot fungi) were able to produce oxalic acid, regardless of whether CaCO₃ was present in the medium. Strains of the other group (mostly white-rot fungi) were characterized by their ability to produce oxalic acid only when CaCO₃ was added to the medium. With the latter group, shake-culturing was generally more effective than stationary culturing in respect to acid production. In the CaCO₃-containing media, Schizophyllum commune, Merulius tremellosus, and Porodisculus pendulus were found to produce substantial amounts of L-malic acid as a main metabolic product, along with small quantities of oxalic and other acids in shake cultures. Especially, S. commune and M. tremellosus may be employed as malic acid-producing species.     

In Vitro Growth of Acremonium coenophialum, an Endophyte of Toxic Tall Fescue Grass

Acremonium coenophialum, an endophytic fungus present in toxic tall fescue grass and seed, grew very slowly or not at all with conventional media and cultural practices. However, a considerable increase in growth was achieved in a relatively dilute medium consisting solely of glucose and yeast extract. The optimal levels of glucose and yeast extract were 3 to 6% and 0.35% (wt/vol), respectively. The addition of salts which lowered the pH suppressed growth. Even when the pH was controlled, the addition of KH₂PO₄ at a level of 3.2% or more greatly inhibited growth. A. coenophialum grew better in shake culture than in stationary culture. The optimal temperature was 23°C, and the optimal pH was 6.5.     

Comparison of bacteriocins production from Enterococcus faecium strains in cheese whey and optimised commercial MRS medium

The production of bacteriocins from cheap substrates could be useful for many food industrial applications. This study aimed at determining the conditions needed for optimal production of enterocins SD1, SD2, SD3 and SD4 secreted by Enterococcus faecium strains SD1, SD2, SD3 and SD4, respectively. To our knowledge, this is the first use of cheese whey—a low-cost milk by-product—as a substrate for bacteriocin production by E. faecium; skimmed milk and MRS broths were used as reference media. This cheese manufacturing residue proved to be a promising substrate for the production of bacteriocins. However, the levels of secreted antimicrobial compounds were lower than those achieved by E. faecium strains in MRS broth. Bacteriocin production was affected strongly by physical and chemical factors such as growth temperature, time of incubation, pH, and the chemical composition of the culture medium. The optimal temperature and time of incubation supporting the highest bacteriocin production was determined for each strain. Different types, sources and amounts of organic nitrogen, sugar, and inorganic salts played an essential role in bacteriocin secretion. E. faecium strains SD1 and SD2—producing high bacteriocin levels both in cheese whey and skimmed milk—could be of great interest for potential applications in cheese-making.     

Development of a low-cost medium for production of nisin from Lactococcus lactis subsp. lactis

The goal of this project was to develop a lower-cost medium for nisin production, so this bacteriocin could be used in a broader range of industrial fermentation processes. The objectives included: (1) evaluating methods for controlling the inhibitory effect of lactic acid produced during fermentation, and (2) comparing two inexpensive complex media for nisin production. Lactococcus lactis subsp. lactis was cultured in shake flasks on Laurel–Tryptose broth to evaluate a range of buffers for pH control. NaHCO₃ proved to be an effective buffer for increasing nisin production. Subsequent trials then evaluated condensed corn soluble (CCS, a fuel ethanol production byproduct) and cheese whey as inexpensive growth media. CCS was shown to be an efficient, low-cost medium for high nisin titers and yields. These modifications reduced the medium costs for nisin production from $600/kg nisin (based on Laurel–Tryptose broth medium) to $35–40/kg nisin for the corn solubles medium.     

Appraisal of Media and Methods for Assay of Bacteriophages of Lactic Streptococci

To assess the relative merits of tryptone yeast extract agar, the same medium unbuffered, and medium M17 for the assay of nine bacteriophages of lactic streptococci, comparative plaque counts were made with an overlay of 3 or 9 ml. Four of the phages exhibited no significant difference in plating efficiency between media. The effect of overlay volume varied from strain to strain and was different for different media. The 3-ml overlay created suboptimal atmospheric conditions for those strains which had a special requirement for CO₂. The use of a 9-ml overlay obviated the need to incubate plates under CO₂ and overcame the problems related to special calcium requirements when tryptone yeast extract agar was used. The organic buffer (disodium β-glycerophosphate) was inhibitory to Streptococcus cremoris ML1 and showed no advantage over the inorganic phosphate buffer (K₂HPO₄) for most other strains.     

Pediocin production by recombinant lactic acid bacteria

Production of the anti-listerial bacteriocin, pediocin, by lactic acid bacteria (LAB) transformed with the cloning vector pPC418 (Ped⁺, 9.1 kb) was influenced by composition of media and incubation temperature. Maximum pediocin production, tested against Listeria innocua, by electrotransformants of Lactococcus lactis ssp. lactis was measured in tryptone/lactose/yeast extract medium after 24 h growth at 30 °C, while incubation at 40 °C was optimum for Ped⁺ transformants of Streptococcus thermophilus and Enterococcus faecalis. The amount of pediocin produced by S. thermophilus in skim milk and cheese whey supplemented with 0.5% yeast extract was estimated as 51000 units ml^–1 and 25000 units ml^–1, respectively. Pediocin production remained essentially unchanged in reconstituted skim milk or whey media diluted up to 10-fold. The results demonstrate the capacity of recombinant strains of LAB to produce pediocin in a variety of growth media including skim milk and inexpensive cheese whey-based media, requiring minimum nutritional supplementation.     

Induction of Calcium Carbonate by Bacillus cereus

The purpose of this research was to study how the bacteria Bacillus cereus (DCB1) utilizes calcium ions in a culture medium with carbon dioxide (CO₂) to yield calcium carbonate (CaCO₃). The bacteria strain DCB1 was a dominant strain isolated from dolomitic surfaces in areas of Karst topographies. The experimental method was as follows: a modified beef extract-peptone medium (beef extract 3.0 g, peptone 10 g, NaCl 5.0 g, CaCl₂ 2.0 g, glass powder 2.0 g, distilled water 1 L, and a pH between 6.5 and 7.5) was inoculated with B. cereus to attempt to induce the synthesis of CaCO₃. The sample was then processed by centrifugation every 24 h during the 7-day cultivation period. The pH, carbonic anhydrase (CA) activity, and the concentrations of both HCO^- ₃ and Ca²⁺ in the supernatant fluid were measured. Subsequently, precipitation in the culture medium was analyzed to confirm, or otherwise, the presence and if present, the formation, of CaCO₃. Methods used included X-ray diffraction (XRD), Scanning Electron Microscopy (SEM), Transmission Electron Microscopy (TEM), and Energy Dispersive Spectroscopy (EDS). Meanwhile, the carbon source in the carbonate was classified by its isotope composition. Results showed that B. cereus can improve its pH value in this culture medium; concentrations of HCO^- ₃ and Ca²⁺ showed a significant decline over the duration of the cultivation period. CA activity reached its maximum during the second day; XRD, SEM, TEM, and isotope analysis all revealed the presence of CaCO₃ as a precipitate. Additionally, these results did not occur in an aseptic control group: no detectable level of CaCO₃ was produced therein. In conclusion: B. cereus can metabolize active materials, such as secretase, by its own growth and metabolism, and can either utilize atmospheric CO₂, or respire, to induce CaCO₃ production. Experimental evidence is offered for a concomitant CO₂ reduction and CaCO₃ induction by microorganisms.     

Optimization of culture media for L-asparaginase production by newly isolated bacteria,Bacillus sp. GH5

The enzyme L-asparaginase has been extensively studied by many researchers mainly because of its considerable therapeutic properties. Producing a convenient quantity of L-asparaginase can be conducted either by discovering new microbial sources with higher enzyme production or by manipulating the medium components for known microbial sources. The present paper discusses the studies carried out in order to enhance the production of L-asparaginase by newly isolated bacteria, Bacillus sp. GH5. Based on the results obtained from media optimization studies, a modified media was developed for optimal L-asparaginase production. Concisely, screening of the nutrients using a proper statistical design showed that tapioca starch, gelatin, ammonium oxalate, CaCO₃, and L-asparagine were respectively the most important sources for carbon, organic nitrogen, inorganic nitrogen, mineral salt, and amino acids. The composition of the optimized medium was the following (per 1 L): 5.0 g L-asparagine; 0.5 g MgSO₄ · 7H₂O; 6.0 g NaHPO₄ · 2H₂O; 3.0 g (NH₄)₂C₂O₄; 0.5 g CaCO₃; 0.014 g CaCl₂ · 2H₂O; 2.0% w/v tapioca starch; 5.0 g gelatin; and 15.0 g agar.     

Use of glycerol for producing 1,3-dihydroxyacetone by Gluconobacter oxydans in an airlift bioreactor

1,3-Dihydroxyacetone can be produced by biotransformation of glycerol with glycerol dehydrogenase from Gluconobacter oxydans cells. Firstly, improvement the activity of glycerol dehydrogenase was carried out by medium optimization. The optimal medium for cell cultivation was composed of 5.6 g/l yeast extract, 4.7 g/l glycerol, 42.1 g/l mannitol, 0.5 g/l K₂HPO₄, 0.5 g/l KH₂PO₄, 0.1 g/l MgSO₄·7H₂O, and 2.0 g/l CaCO₃ with the initial pH of 4.9. Secondly, an internal loop airlift bioreactor was applied for DHA production from glycerol by resting cells of G. oxydans ZJB09113. Furthermore, the effects of pH, aeration rate and cell content on DHA production and glycerol feeding strategy were investigated. 156.3 ± 7.8 g/l of maximal DHA concentration with 89.8 ± 2.4% of conversion rate of glycerol to DHA was achieved after 72 h of biotransformation using 10 g/l resting cells at 30 °C, pH 5.0 and 1.5 vvm of aeration rate.