Specific Interaction of the Unmodified Bacteriocin Lactococcin 972 with the Cell Wall Precursor Lipid II

Lactococcin 972 (Lcn972) is a nonlantibiotic bacteriocin that inhibits septum biosynthesis in Lactococcus lactis rather than forming pores in the cytoplasmic membrane. In this study, a deeper analysis of the molecular basis of the mode of action of Lcn972 was performed. Of several lipid cell wall precursors, only lipid II antagonized Lcn972 inhibitory activity in vivo. Likewise, Lcn972 only coprecipitated with lipid II micelles. This bacteriocin inhibited the in vitro polymerization of lipid II by the recombinant S. aureus PBP2 and the addition to lipid II of the first glycine catalyzed by FemX. These experiments demonstrate that Lcn972 specifically interacts with lipid II, the substrate of both enzymes. In the presence of Lcn972, nisin pore formation was partially hindered in whole cells. However, binding of Lcn972 to lipid II could not compete with nisin in lipid II-doped 1,2-dioleoyl-sn-glycero-3-phosphocholine (DOPC) liposomes, possibly indicating a distinct binding site. The existence of a putative cotarget for Lcn972 activity is discussed in the context of its narrow inhibitory spectrum and the localized action at the division septum. To our knowledge, this is the first unmodified bacteriocin that binds to the cell wall precursor lipid II.     

Effects of cultivation conditions on the production of heterologous α-galactosidase by Kluyveromyces lactis

Growth conditions relevant for the large-scale production of heterologous proteins with yeasts were studied on a laboratory scale. A strain of Kluyveromyces lactis, containing 15 copies of an expression cassette encoding guar -galactosidase integrated into its ribosomal DNA, was used as a model. By using urea as a nitrogen source, it was possible to produce active extracellular -galactosidase in shake-flask cultures grown on a defined mineral medium. Inclusion of urea instead of ammonium sulphate prevented unwanted acidification of cultures. With urea-containing mineral medium, enzyme production in shake flasks was comparable to that in complex media containing peptone. In contrast, the presence of peptone was required to achieve high productivity in chemostat cultures. The low productivity in chemostat cultures growing on mineral media was not due to loss oft the expression cassette, since addition of peptone to such cultures resulted in an immediate high rate of -galactosidase production. The discrepancy between the behaviour of shake-flask and chemostat cultures during growth on mineral medium illustrates the necessity of physiological studies for the scalling-up of heterologous protein production from laboratory to production scale.     

Nisin Z produced by <Emphasis Type="Italic">Lactococcus lactis</Emphasis> from bullfrog hatchery is active against <Emphasis Type="Italic">Citrobacter freundii</Emphasis>, a red-leg syndrome related pathogen

Lactococcus lactis subsp. lactis CRL 1584 isolated from a bullfrog hatchery produces a bacteriocin that inhibits both indigenous Citrobacter freundii (a Red-Leg Syndrome related pathogen) and Lactobacillus plantarum, and Listeria monocytogenes as well. Considering that probiotics requires high cell densities and/or bacteriocin concentrations, the effect of the temperature on L. lactis growth and bacteriocin production was evaluated to find the optimal conditions. Thus, the growth rate was maximal at 36 °C, whereas the highest biomass and bacteriocin activity was achieved between 20 and 30 °C and 20–25 °C, respectively. The bacteriocin synthesis was closely growth associated reaching the maximal values at the end of the exponential phase. Since bacteriocins co-production has been evidenced in bacterial genera, a purification of the bacteriocin/s from L. lactis culture supernatants was carried out. The active fraction was purified by cationic-exchange chromatography and then, a RP-HPLC was carried out. The purified sample was a peptide with a 3353.05 Da, a molecular mass that matches nisin Z, which turned out to be the only bacteriocin produced by L. lactis CRL 1584. Nisin Z showed bactericidal effect on C. freundii and L. monocytogenes, which increased in the presence l-lactic acid?+?H₂O₂. This is the first report on nisin Z production by L. lactis from a bullfrog hatchery that resulted active on a Gram-negative pathogen. This peptide has potential probiotic for raniculture and as food biopreservative for bullfrog meat.     

Heterotrophic growth of Thiobacillus acidophilus in batch and chemostat cultures

Heterotrophic growth of the facultatively chemolithoautotrophic acidophile Thiobacillus acidophilus was studied in batch cultures and in carbon-limited chemostat cultures. The spectrum of carbon sources supporting heterotrophic growth in batch cultures was limited to a number of sugars and some other simple organic compounds. In addition to ammonium salts and urea, a number of amino acids could be used as nitrogen sources. Pyruvate served as a sole source of carbon and energy in chemostat cultures, but not in batch cultures. Apparently the low residual concentrations in the steady-state chemostat cultures prevented substrate inhibition that already was observed at 150 M pyruvate. Molar growth yields of T. acidophilus in heterotrophic chemostat cultures were low. The Y _max and maintenance coefficient of T. acidophilus grown under glucose limitation were 69 g biomass · mol^–1 and 0.10 mmol · g^–1 · h^–1, respectively. Neither the Y _max nor the maintenance coefficient of glucose-limited chemostat cultures changed when the culture pH was increased from 3.0 to 4.3. This indicates that in T. acidophilus the maintenance of a large pH gradient is not a major energy-requiring process. Significant activities of ribulose-1,5-bisphosphate carboxylase were retained during heterotrophic growth on a variety of carbon sources, even under conditions of substrate excess. Also thiosulphate- and tetrathionate-oxidising activities were expressed under heterotrophic growth conditions.     

Chemostat production of pediocin SM‐1 by Pediococcus pentosaceus Mees 1934

Production of the bacteriocin pediocin SM‐1 by Pediococcus pentosaceus Mees 1934 was investigated in pH‐controlled batch and chemostat cultures using a complex medium containing glucose, sucrose or fructose. In chemostat cultures operated at 150 rpm, 30°C, 60% dissolved oxygen tension, pH 6.5, and D = 0.148 h^?1, the pediocin titer reached 185 AU/mL representing an increase of 32% compared with batch cultures in which glucose was used as the carbon source. Pediocin biosynthesis was markedly affected by the growth rate of the producer microorganism. For all carbon sources tested, pediocin production appeared to take place only at dilution rates lower than μ_max. However, only glucose supported production at the very low dilution rate of 0.05 h^?1 indicating a direct regulation of pediocin biosynthesis by the carbon source. Glucose supported higher biomass productivity and higher pediocin titers and yields compared with the other sugars used. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1481–1486, 2015     

The effect of thiosulphate and other inhibitors of autotrophic nitrification on heterotrophic nitrifiers

It has been found that heterotrophic nitrification by Thiosphaera pantotropha can be inhibited by thiosulphate in batch and chemostat cultures. Allythiourea and nitrapyrin, both classically considered to be specific inhibitors of autotrophic nitrification, inhibited nitrification by Tsa. pantotropha in short-term experiments with resting cell suspensions. Hydroxylamine inhibited ammonia oxidation in chemostat cultures, but was itself fully oxidized. Thus the total nitrification rate for the culture remained the same.Heterotrophic nitrification by another organism, a strain of Pseudomonas denitrificans has also been shown to be inhibited by thiosulphate in short term experiments and in the chemostat. During these experiments it became evident that this strain is able to grow mixotrophically (with acetate) and autotrophically in a chemostat with thiosulphate as the energy source.     

The influence of limiting and non-limiting growth conditions on glucose and maltose metabolism in Lactococcus lactis ssp. lactis strains

Three strains of Lactococcus lactis ssp. lactis, a dairy strain 65.1, a type strain ATCC 19435, and a mutant AS 211, were grown on glucose and on maltose under chemostat conditions. When the culture was shifted from glucose-limiting to non-limiting conditions, the product shifted from mixed acids to lactate. Mixed acids were obtained in all maltose cultures; however, an enhanced lactate formation was observed in 19435 and AS 211. An inorganic-phosphate (P_i)-dependent maltose phosphorylase activity was found to be responsible for the initial conversion of maltose. The activation of maltose phosphorylase by Pi was strain-specific. When growth was on maltose under non-limiting conditions, a correlation was found between high initial maltose phosphorylase and -phosphoglucomutase activities and lactate production. No such correlation was observed in maltose-limited cells. In glucose-grown cells under non-limiting conditions, homo-fermentative lactate formation coincided with high concentrations of fructose 1,6-bisphosphate (Fru1,6P ₂) and pyruvate (Pyr) and low concentrations of phosphoenolpyruvate (PPyr). Under limiting conditions, mixed acid formation coincided with low concentrations of Fru1,6P ₂ and Pyr and high concentrations of PPyr. In maltose-grown cells there was no correlation between intracellular intermediary metabolite concentrations and product formation. Therefore, in addition to intracellular intermediary metabolite concentrations, the product formation on maltose is suggested to be regulated by the transport and initial phosphorylating steps.     

Modeling growth,lipid accumulation and lipid turnover in submerged batch cultures of <Emphasis Type="Italic">Umbelopsis isabellina</Emphasis>

The production of lipids by oleaginous yeast and fungi becomes more important because these lipids can be used for biodiesel production. To understand the process of lipid production better, we developed a model for growth, lipid production and lipid turnover in submerged batch fermentation. This model describes three subsequent phases: exponential growth when both a C-source and an N-source are available, carbohydrate and lipid production when the N-source is exhausted and turnover of accumulated lipids when the C-source is exhausted. The model was validated with submerged batch cultures of the fungus Umbelopsis isabellina (formerly known as Mortierella isabellina) with two different initial C/N-ratios. Comparison with chemostat cultures with the same strain showed a significant difference in lipid production: in batch cultures, the initial specific lipid production rate was almost four times higher than in chemostat cultures but it decreased exponentially in time, while the maximum specific lipid production rate in chemostat cultures was independent of residence time. This indicates that different mechanisms for lipid production are active in batch and chemostat cultures. The model could also describe data for submerged batch cultures from literature well.     

Isolation of Lactococcus lactis mutants simultaneously resistant to the cell wall-active bacteriocin Lcn972, lysozyme, nisin, and bacteriophage c2

Lactococcin 972 (Lcn972) is a nonlantibiotic bacteriocin that inhibits cell wall biosynthesis by binding to lipid II. In this work, two mutants resistant to Lcn972, Lactococcus lactis D1 and D1-20, with high (>320 arbitrary units [AU]/ml) and low (80 AU/ml) susceptibilities, respectively, have been isolated. Resistance to Lcn972 did not impose a burden to growth under laboratory conditions, nor did it substantially alter the physicochemical properties of the cell surface. However, the peptidoglycan of the mutants featured a higher content of muropeptides with tripeptide side chains than the wild-type strain, linking for the first time peptidoglycan remodelling to bacteriocin resistance. Moreover, L. lactis lacking a functional D,D-carboxypeptidase DacA (i.e., with a high content of pentapeptide side chain muropeptides) was shown to be more susceptible to Lcn972. Cross-resistance to lysozyme and nisin and enhanced susceptibility to penicillin G and bacitracin was also observed. Intriguingly, the Lcn972-resistant mutants were not infected by the lytic phage c2 and less efficiently infected by phage sk1. Lack of c2 infectivity was linked to a 22.6-kbp chromosomal deletion encompassing the phage receptor protein gene pip. The deletion also included maltose metabolic genes and the two-component system (TCS) F. However, a clear correlation between these genes and resistance to Lcn972 could not be clearly established, pointing to the presence of as-yet-unidentified mutations that account for Lcn972 resistance.     

Regulation of proteinase synthesis in Lactococcus lactis

The synthesis of extracellular serine proteinase of Lactococcus lactis was studied during the growth in a batch and a continuous culture on chemically defined media. In a batch culture the proteinase synthesis started during the exponential phase of growth and the highest proteinase concentrations were found at the end of the exponential and beginning of the stationary phase of growth. During the growth in a lactose-limited chemostat with amino acids as the sole source of nitrogen, the specific rate of proteinase synthesis was maximal at a μof 0.23 h^?1. At higher growth rates the proteinase productin declined. The proteinase synthesis was dependent on the amino acid sources in the medium. In batch cultures of L. lactis grown on a chemically defined medium with amino acids, the proteinase production was increased four-fold compared to media containing casein or a tryptic digest of casein as the sole source of nitrogen. The inhibition of the rate of proteinase synthesis by casein and peptides was also observed during the growth in a chemostat. The addition of the dipeptide leucylproline (final concentration of 100 μM) to a lactose-limited continuous culture during the steady state (D = 0.23 h^?1) resulted in a transient inhibition of the rate of proteinase synthesis. This suggested that exogenously supplied peptides control the regulation of proteinase synthesis of L. lactis.     

Influence of pH on growth and bacteriocin production byLactococcus lactis subsp.lactis 14ONWC during batch fermentation

The influence of pH on growth, and lactic acid and bacteriocin production byLactococcus lactis subsp.lactis 140 NWC was studied during batch fermentation in a lactose-based complex medium. Growth and lactic acid production were modelled using a simple logistic equation while substrate consumption was found to be a function growth and lactic acid production rate. The optimal pH for growth and lactic acid production was between 6.0 and 6.5. Bacteriocin production showed primary metabolite kinetics. pH had a dramatic effect on the production of the bacteriocin, lactococcin 140. A maximum activity of 15.4 × 10⁶ AU (arbitrary units) 1^–1 was obtained after 7 h at pH 5.5. Maximum bacteriocin activity was achieved before the end of growth and was followed by a decrease in activity, which was due to adsorption to the cells of the producing organism, possibly followed by degradation by specific proteases. Both bacteriocin production and degradation rates were higher at pH 5.0 and 5.5, resulting in sharper activity peaks than at pH 6.0 or 6.5. On the basis of the experimental results a qualitative model for bacteriocin production is proposed.     

Modeling the batch bacteriocin production system by lactic acid bacteria by using modified three-dimensional Lotka–Volterra equations

Different batch cultures of Lactococcus lactis CECT 539, a nisin-producing strain, were carried out in culture media prepared with whey and mussel processing wastes. From these cultures, a reasonable system of differential equations, similar to the three-dimensional Lotka–Volterra two predators-one prey model, was set up to describe, for the first time, the relationship between the absolute rates of growth, pH drop and nisin production.Thus, the nisin production system was described as a three-species (pH, biomass and nisin) ecosystem. In this case, both nisin and biomass production were considered as two pH-dependent species that compete for the nitrogen source. Excellent agreement (R² values ≥0.9885) resulted between model predictions and the experimental data, and significant values for all the model parameters were obtained. The developed model was demonstrated (R² values ≥0.9874) for five batch cultivations of the strains L. lactis CECT 539 in MRS broth and Lactobacillus sakei LB 706 (sakacin A producer), Pediococcus acidilactici LB42-923 (pediocin AcH producer), L. lactis ATCC 11454 (nisin producer) and Leuconostoc carnosum Lm1 (leuconocin Lcm1 producer) in TGE broth. These results suggest that the batch bacteriocin production system in these culture media can be successfully described by using the Lotka–Volterra approach.     

Influence of the phosphorus and nitrogen source on nisin production in Lactococcus lactis subsp. lactis batch fermentations using a complex medium

The influence of different phosphorus and nitrogen sources on Lactococcus lactis subsp. lactis NIZO 22186 growth and nisin production was studied in batch fermentations using a complex medium. KH₂PO₄ was found to be the best phosphorus source for nisin production. Increasing initial phosphate concentrations from 0 to 5% KH₂PO₄ exerted a double effect, creating favourable pH conditions and particularly stimulating the nisin production levels, which were highest at 5% KH₂PO₄. Up to now, no such high initial phosphate concentrations have been reported for the production of other antibiotics or bacteriocins. Nisin, a lanthionine-containing peptide antibiotic with bacteriocin properties, clearly behaved as a primary metabolite, since its formation was linked with active growth and was not suppressed by phosphate concentrations up to 5%. A complex medium supplemented with cotton seed meal as nitrogen source also gave very high nisin yields. Correspondence to: L. De Vuyst     

Expression of<Emphasis Type="Italic"> Sulfolobus solfataricus</Emphasis> α-glucosidase in<Emphasis Type="Italic"> Lactococcus lactis</Emphasis>

The industrial potential to use extreme thermophilic microorganisms and their enzymes lies in applications in which the temperature cannot be adjusted (cooled) at will. The production of enzymes from wild-type thermophiles is very low, therefore, for industrial applications, it is necessary to use recombinant microorganisms. In this paper, the cloning of a heat-stable -glucosidase from Sulfolobus solfataricus using lactic acid bacteria as expression system is reported. The extremophilic -glucosidase was cloned in Lactococcus lactis and correctly folded despite being expressed at a lower temperature. The recombinant cells were assayed for enzyme residual activity at 75 °C in order to analyze the direct use of whole cells as biocatalysts. Maximum activity corresponded to 40 U/l in static cultures. The protein yield was further improved by optimizing fermentation and reached 600 U/l in batch mode. Microfiltration led to an even higher enzyme production of 850 U/l as a result of increased biomass. The overall production of -glucosidase using the engineered L. lactis strain in microfiltration fermentation is 1,000-fold higher than obtained using the wild-type.     

The growth of Pseudomonas putida on m-toluic acid and on toluene in batch and in chemostat cultures

Summary The present study describes the growth of Pseudomonas putida cells (ATCC 33015) in batch and continuous cultures on two toxic substrates; toluene and m-toluic acid as sole carbon and energy sources. In fed-batch cultures on m-toluic acid up to 3.55 g cell dry weight/1 were achieved with a maximal specific growth rate (_max) of 0.1 h^-1. The average cellular yield was 1.42 g cell dry weight/g m-toluic acid utilized. When liquid toluene was added to shake-flask cultures in the presence of 0.7 g/1 m-toluic acid, the average cellular yield obtained was 1.3 g cell dry weight/g toluene utilized and the _max was 0.13 h^-1. Growth on toluene vapour in the presence of 0.7 g/l m-toluic acid in batch cultures resulted in a cellular yield of 1.28 g cell dry weight/g toluene utilized, with growth kinetics almost identical to those with liquid toluene (_max liquid=0.13 h^-1, _max vapour=0.12 h^-1). The maximal biomass concentration was 3.8 g cell dry weight/l, obtained in both cases after 100 h of incubation. Pseudomonas putida was grown in a chemostat initially on 0.7 g/l m-toluic acid and vapour toluene and then in the steady state on toluene as the sole source of carbon and energy. Toluene was added continuously to the culture as vapour with the inflowing airstream. Chemostat cultures could be maintained at steady state for several months on toluene. The maximal biomass concentration obtained in the chemostat culture was 3.2 g cell dry weight/l. The maximum specific growth rate was 0.13 h^-1, with a cellular yield of 1.05 g cell dry weight/g toluene utilized. Approximately 70% of the toluene consumed was converted into biomass, and the remainder was converted to CO₂ and unidentified byproducts.     

The production of α-amylase in batch and chemostat culture by Bacillus stearothermophilus

The production of -amylase (-1,4-glucan 4-glucanohydrolase; EC. 3.2.1.1) by a strain of Bacillus stearothermophilus isolated from leaf litter was investigated in a tryptone-maltose medium at 55°C in batch and chemostat culture. Amylase production was growth-limited and restricted to the exponential phase in batch culture. The enzyme yield was reduced by 40% when the culture pH was maintained at pH 7.2. Amylase production in chemostat culture was influenced by the growth rate throughout the dilution rate range used.     

α-Amylase production by Bacillus amyloliquefaciens in a membrane recycle bioreactor

A strain of Bacillus amyloliquefaciens was cultivated in a membrane recycle bioreactor for the production of an extracellular -amylase. Continuous cultivations of B. amyloliquefaciens in the recycle fermentor led to higher cell mass and volumetric productivities than the ones obtained in batch or chemostat cultivations; the -amylase activities were lower than in the batch mode but significantly higher than in the chemostat mode. The operation of the membrane recycle bioreactor was sometimes disturbed by high broth viscosity leading to a stronger fouling of the membrane.     

Growth and energy production in Bacteroides amylophilus

The molar growth yield (Y _m) of Bacteroides amylophilus strain WP91 on maltose was 68±2 g/mol when determined from batch cultures at the peaks of maximal growth. Continued incubation led to considerable cell lysis. When calculated from batch cultures in exponential phase (specific growth rate, =0.57 h^-1) Y _m was 101 g/mol. The maximum value of Y _m in maltose-limited chemostat cultures at the maximum dilution rate (D) attainable (D==0.39 h^-1) was about 79 g/mol. Ammonia-Fmited chemostat cultures metabolized maltose with a much reduced efficiency and this was associated with a difference in morphology and chemical composition of the cells. The theoretical maximum molar growth yields (Y _m ^max ) were 55 and 114 g/mol for ammonia- and maltose-limited growth respectively. However, if account was taken of extracellular nitrogen-containing material in ammonia-limited cultures, Y _m ^max became 60. The maintenance coefficient (m _s), estimated from the lines relating the specific rate of maltose consumption (q _m) and D (where m _s=q _m at D=0), was 7.4±0.6×10^-4 mol maltose/g x h for both nutrient limitations. A difference in maintenance energy demand, independent of growth-rate, could not account, therefore, for the observed differences in Y _m between ammonia- and maltose-limited growth.