Growth and Energy Generation by Lactococcus lactis subsp. lactis biovar diacetylactis during Citrate Metabolism

Growth of Lactococcus lactis subsp. lactis biovar diacetylactis was observed on media with citrate as the only energy source. At pH 5.6, steady state was achieved in a chemostat on a citrate-containing medium in the absence of a carbohydrate. Under these conditions, pyruvate, acetate, and some acetoin and butanediol were the main fermentation products. This indicated that energy was conserved in L. lactis subsp. lactis biovar diacetylactis during citrate metabolism and presumably during the conversion of citrate into pyruvate. The presumed energy-conserving step, decarboxylation of oxaloacetate, was studied in detail. Oxaloacetate decarboxylase was purified to homogeneity and characterized. The enzyme has a native molecular mass of approximately 300 kDa and consists of three subunits of 52, 34, and 12 kDa. The enzyme is apparently not sodium dependent and does not contain a biotin moiety, and it seems to be different from the energy-generating oxaloacetate decarboxylase from Klebsiella pneumoniae. Energy-depleted L. lactis subsp. lactis biovar diacetylactis cells generated a membrane potential and a pH gradient immediately upon addition of citrate, whereas ATP formation was slow and limited. In contrast, lactose energization resulted in rapid ATP formation and gradual generation of a proton motive force. These data were confirmed during studies on amino acid uptake. α-Aminoisobutyrate uptake was rapid but glutamate uptake was slow in citrate-energized cells, whereas lactose-energized cells showed the reverse tendency. These data suggest that, in L. lactis subsp. lactis bv. diacetylactis, a proton motive force could be generated during citrate metabolism as a result of electrogenic citrate uptake or citrate/product exchange together with proton consumption by the intracellular oxaloacetate decarboxylase.     

Cross-Feeding of Lactate Between Streptococcus lactis and Bacteroides sp. Isolated from Termite Hindguts

Streptococcus lactis and Bacteroides sp., isolated from hindguts of Reticulitermes flavipes termites, were grown anaerobically in monoculture and coculture. When grown in a glucose medium, S. lactis monoculture produced lactate as the major fermentation product, with small amounts of formate, acetate, ethanol, and CO₂. In coculture, glucose was completely consumed during growth of S. lactis. Lactate, produced by S. lactis, then supported much of the growth of Bacteroides and was fermented to propionate, acetate, and CO₂. Small amounts of succinate were formed during growth of Bacteroides in the coculture, but little change in the formate or ethanol concentration was observed. Monoculture growth of Bacteroides in a tryptone-yeast extract medium revealed that incorporation of 20 to 40 mM lactate increased cell yields and production of organic acids. However, initial lactate concentrations greater than 40 mM suppressed not only growth of Bacteroides but also acidic product formation. Results suggest that cross-feeding of lactate between streptococci and bacteroides constitutes one aspect of the overall hindgut fermentation in termites.     

Diacetyl production by different strains of Lactococcus lactis subsp. lactis var. diacetylactis and Leuconostoc spp.

Summary Several strains of Lactococcus lactis subsp. lactis var. diacetylactis and Leuconostoc spp. were compared for product formation from citrate in milk cultures. Most strains produced acetoin and butanediol. Some strains derived from buffer starter cultures produced, in addition, -acetolactate. Lactococcus lactis strain C17, which produced acetoin and butanediol but no -acetolactate in culture, was compared physiologically with L. lactis strain Ru4, which produced only -acetolactate. Activities of enzymes involved in citrate metabolism were almost identical in both strains, with the exception of -acetolactate decarboxylase, which was missing in strain Ru4. The formation of -acetolactate, acetoin and diacetyl was further analysed in cell-free extracts. -Acetolactate synthase activity saturated at a high pyruvate concentration (100 mm). This is in agreement with the observed accumulation of pyruvate externally, and probably internally, during -acetolactate, acetoin and butanediol production by L. lactis cells.Correspondence to: J. Hugenholtz     

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.     

Generalized model of the effect of pH on lactate fermentation and citrate bioconversion in Lactococcus lactis ssp. Lactis biovar. diacetylactis

An aroma-imparting mesophilic lactic starter (Lactococcus lactis ssp. lactis biovar. diacetylactis) was studied in batch culture in medium with 50 g·l^–1 lactose and 2 g·l^–1 citrate. The effect of pH on the physiology of growth and the production of flavour compounds was investigated with a mathematical model. The specific rates of growth and of lactose fermentation obeyed a law of non-competitive inhibition by lactic acid produced, inhibition increasing as the pH of the medium decreased. The pH thus acted indirectly by increasing the proportion of non-dissociated lactic acid, identified as the inhibiting form of lactic acid. The generalized model, taking into account the effect of pH, was tested using fermentations at pH controlled at different values (4.5–6.5), as well as with a fermentation conducted at non-regulated pH. These simulations supported the working hypotheses. The effect of pH on the fermentation of citric acid resulted in an increase in the maximal specific rate of citrate utilization, in the bioconversion yield, and in the constant of diacetyl and acetoin reduction at acid pH. The production of flavour compounds is a complex phenomenon resulting from the interaction of pH, citric acid concentration, and the physiological state of the cells. These results are discussed with respect to the use of this strain in the preparation of manufactured dairy products.     

Quantification of citrate lyase by enzyme-linked immunosorbent assay for determining the population of Lactococcus lactis subsp. Lactis biovar diacetylactis in pure and mixed cultures

Citrate lyase production by Lactococcus lactis subsp. lactis biovar diacetylactis DRC2 was quantified by an enzyme-linked immunosorbent assay (ELISA). The citrate lyase reached a concentration equivalent to 41 ± 4 g/ml purified citrate lyase in pure culture. When the strain DRC2, grown in mixed culture with L. lactis subsp. cremoris AM2, represented around 70% (DC culture) or 30% (CD culture) of the total initial population, the level of citrate lyase decreased to 21 ± 7 g/ml and 4.5 ± 1.5 g/ml respectively. The maximum bacterial concentration of strain DRC2 in pure culture reached 2.6 × 10⁹ cfu/ml and decreased to 1.5 (± 0.2) × 10⁹ cfu/ml and 0.5 (± 0.3) × 10⁹ cfu/ml in DC and CD mixed cultures respectively. In mixed cultures, the proportion of the strain DRC2 was 8.5 ± 5.0% lower at the end of the fermentation than immediately after inoculation, thus showing that this strain was clearly inhibited. However, the maximum rate of citrate consumption was the same during pure DRC2 culture and CD mixed culture (2.5 ± 0.3 mmol/h) and slightly highre in DC culture (3.07 mmol/h). The maximum rate of acidification was 0.37 ± 0.04 pH unit/h regardless of the culture. A good correlation was obtained between the population of the strain DRC2 and the citrate lyase concentration determined by ELISA but no relationship was found between citrate consumption and citrate lyase synthesis. Therefore an ELISA test of this kind can be used to monitor the growth of L. lactis subsp. lactis biovar diacetylactis in mixed cultures.     

Enzymatic methods for determining populations of Streptococcus cremoris AM2 and Leuconostoc lactis CNRZ 1091 in pure and mixed cultures

Summary Streptococcus cremoris AM2 is characterized by an aminopeptidase and Leuconostoc lactis CNRZ 1091 by an -galactosidase and a citrate lyase. These strains were grown in pure or mixed cultures, in presence or absence of citrate (15 mM) and at controlled or uncontrolled pH. Cell populations and the activities of the enzymes were measured during microbial growth. Linear correlations were established between the population of S. cremoris AM2 and aminopeptidase activity, and between that of L. lactis CNRZ 1091 and the activities of -galactosidase and citrate lyase. These correlations held regardless of whether the culture was pure or mixed and if the pH was controlled or not. The presence of citrate did not change citrate lyase and aminopeptidase activities, but inhibited the synthesis of the -galactosidase and not its activity. The linear relationships permit the determination of bacterial populations in less than 2 h without counting but by measuring enzyme activities.     

Contribution of Citrate Metabolism to the Growth of Lactococcus lactis CRL264 at Low pH

Lactococcus lactis subsp. lactis biovar diacetylactis CRL264 is a natural strain isolated from cheese (F. Sesma, D. Gardiol, A. P. de Ruiz Holgado, and D. de Mendoza, Appl. Environ. Microbiol. 56:2099-2103, 1990). The effect of citrate on the growth parameters at a very acidic pH value was studied with this strain and with derivatives whose citrate uptake capacity was genetically manipulated. The culture pH was maintained at 4.5 to prevent alkalinization of the medium, a well-known effect of citrate metabolism. In the presence of citrate, the maximum specific growth rate and the specific glucose consumption rate were stimulated. Moreover, a more efficient energy metabolism was revealed by analysis of the biomass yields relative to glucose consumption or ATP production. Thus, it was shown that the beneficial effect of citrate on growth under acid stress conditions is not primarily due to the concomitant alkalinization of the medium but stems from less expenditure of ATP, derived from glucose catabolism, to achieve pH homeostasis. After citrate depletion, a deleterious effect on the final biomass was apparent due to organic acid accumulation, particularly acetic acid. On the other hand, citrate metabolism endowed cells with extra ability to counteract lactic and acetic acid toxicity. In vivo ¹³C nuclear magnetic resonance provided strong evidence for the operation of a citrate/lactate exchanger. Interestingly, the greater capacity for citrate transport correlated positively with the final biomass and growth rates of the citrate-utilizing strains. We propose that increasing the citrate transport capacity of CRL264 could be a useful strategy to improve further the ability of this strain to cope with strongly acidic conditions.     

The effect of extracellular pH and lactic acid on pH homeostasis inLactococcus lactis andStreptococcus bovis

WhenStreptococcus bovis JB1 andLactococcus lactis ML3 were grown with an excess of glucose, lactic acid accumulation caused a decrease in extracellular pH;S. bovis grew at extracellular pH values as low as 4.9, butL. lactis was unable to grow below pH 5.3. Because both bacteria maintained a low pH across the cell membrane, it appeared that intracellular pH was controlling their pH sensitivities.S. bovis glycolyzed glucose and maintained high concentrations of ATP at intracellular pH values as low as 5.4.L. lactis could not glycolyze glucose when the intracellular pH was less than 5.6, and ATP declined.L. lactis cells that were washed and incubated in buffers with an excess glucose had higher pH values than growing cells. Lactic acid addition, however, prevented the interconversion of membrane potential () and chemical gradient of protons (ZpH).     

Effects of pH and Sugar on Acetoin Production from Citrate by Leuconostoc lactis

The relationship between acetoin production and citrate utilization in Leuconostoc lactis NCW1 was studied. In a complex medium the organism utilized citrate at neutral pH (initial pH, 6.3) and at acid pH (initial pH, 4.5) but produced nine times more acetoin at the latter pH. In resting cells the utilization of citrate was optimum at pH 5.3. Production of acetoin as a function of citrate utilization increased as the pH decreased, and at pH 4.3 all of the citrate utilized was recovered as acetoin. Glucose (10 mM) and lactose (10 mM) markedly stimulated citrate utilization but totally inhibited acetoin production in glucose- and lactose-grown cells. Addition of glucose to cells actively metabolizing citrate caused an immediate increase in citrate uptake and a reduction in the level of acetoin. The apparent K_m values of lactic dehydrogenase for pyruvate were 1.05, 0.25, and 0.15 mM at pH 7.5, 6.5, and 5.0, respectively. Several heterofermentation intermediates inhibited α-acetolactate synthetase and decarboxylase activities. The implications of these results in regulating acetoin formatin are discussed.     

L-lactate production from xylose employingLactococcus lactis IO-1

Summary The growth, substrate utilisation and L-lactate production ofLactococcus lactis IO-1 were examined on xylose, and glucose and xylose media. The yield of lactate on xylose was 0.47 g lactate/g xylose at an initial xylose concentration of 51.2 g/l and the _max was 0.72 h^–1. Xylose cultures were more susceptible to lactate inhibition than were glucose cultures but showed similar kinetic behaviour. The organism was capable of complete sugar utilisation when grown on a mixture of 20 g/l xylose and 20 g/l glucose and synthesised 0.66 g lactate/g sugar.     

Homo-fermentative production of d-lactic acid by Lactobacillus sp. employing casein whey permeate as a raw feed-stock

Casein whey permeate (CWP), a lactose-enriched dairy waste effluent, is a viable feed stock for the production of value-added products. Two lactic acid bacteria were cultivated in a synthetic casein whey permeate medium with or without pH control. Lactobacillus lactis ATCC 4797 produced d-lactic acid (DLA) at 12.5 g l^?1 in a bioreactor. The values of Leudking–Piret model parameters suggested that lactate was a growth-associated product. Batch fermentation was also performed employing CWP (35 g lactose l^?1) with casein hydrolysate as a nitrogen supplement in a bioreactor. After 40 h, L. lactis produced 24.3 g lactic acid l^?1 with an optical purity >98 %. Thus CWP may be regarded as a potential feed-stock for DLA production.     

Localization of Lactococcus lactis ssp lactis bv diacetylactis in alginate gel beads affects biomass density and synthesis of several enzymes involved in lactose and citrate metabolism

Summary Lactococcus lactis ssp lactis bv diacetylactis, immobilized in calcium alginate beads, was grown in synthetic medium in a continuous flow reactor. Cell distribution inside the gel, as well as the activity of various enzymes, was measured after 30 h of operation. The included biomass tended to concentrate at the periphery of the bead along a section of radius about 100 m long. ATPase activity was maximal in this zone. The activity of NADH oxidase, alcohol dehydrogenase, diacetyl reductase and acetoin reductase, which are repressed in the presence of citrate, were higher in the deeper zones than at the surface of the beads. This result shows that only the peripheral zone of the bead is responsible for the bioconversion of citrate into flavour compounds (diacetyl and acetoin).     

A descriptive model for citrate utilization by Lactococcus lactis ssp lactis bv diacetylactis

A model for the use of citrate by Lactococcus lactis ssp lactis bv diacetylactis CNRZ 125 is proposed. Citrate metabolism by this strain leads to the production of acetate, CO₂ and C4 compounds (diacetyl, acetoin, 2,3-butylene glycol). The model furnishes correct simulations, consistent with published results on the pathways used and on lactose-citrate co-metabolism. Citric acid is incorporated independently of growth. The production of flavoring compounds is a complex process, depending on the rate of citrate utilization, on the proportion of pyruvate arising from citrate and which condenses to form -acetolactate and CO₂, on the rate of transformation of -acetolactate to diacetyl and acetoin, as well as on the rate of reduction of these compounds to 2,3-butylene glycol.     

Comparison of cell wall proteinases from Lactococcus lactis subsp. cremoris AC1 and Lactococcus lactis subsp. lactis NCDO 763

Summary Cell wall-associated proteinases were isolated from Lactococcus lactis subsp. cremoris AC1 and subsp. lactis NCDO 763 in order to compare their specificities towards different caseins. Two purification strategies were applied. Cells grown in casein-free M17 medium were a suitable starting material for purification, since electrophoretic purity could be achieved after one chromatographic step. Both enzymes has an apparent molecular mass of about 145000 daltons as judged by sodium dodecyl sulphate-polyacrylamide gel electrophoresis. Electrophoresis and reversed phase HPLC patterns of hydrolysates of _s1-, _s2-, -, and K-caseins indicated that both proteinases had a similar specificity. The enzyme of L. lactis subsp. lactis split _s1- and _s2-caseins more extensively than that of L. lactis subsp. cremoris.     

Optimization of substrate feed for continuous production of lactic acid by Lactococcus lactis IO-1

Summary Optimization of substrate feed for continuous production of lactic acid by the homofermentative bacterium, Lactococcus lactis IO-1, in glucose medium was investigated. A pH-dependent feed with two pH set-points, a lower set-point for neutralization with alkali and an upper set-point for substrate feed, proved better than continuous substrate feed with one pH set-point for neutralization with alkali only. Built-in electrodialysis with a cell-recycling system was tested and high cell density was achieved as a result of the use of enriched medium. However, specific lactate productivity in this system was not satisfactorily high. pH-dependent feed was combined with turbidity control and a cell recycling. With this system, we achieved high specific lactate productivity of 2 g (g-cell)^-1 h^-1 at a dilution rate of 0.5 h^-1, a dry cell weight of 5 g l ^-1, a level of lactate in the broth of 20 g l ^-1, and a concentration of glucose in the spent medium of about 5 gl ^-1.     

Acetic acid production from whey lactose by the co-culture ofStreptococcus lactis andClostridium formicoaceticum

Summary Acetic acid was produced from anaerobic fermentation of lactose by the co-culture ofStreptococcus lactis andClostridium formicoaceticum at 35° C and pHs between 7.0 and 7.6. Lactose was converted to lactic acid, and then to acetic acid in this mixed culture fermentation. The overall acetic acid yield from lactose was about 95% at pH 7.6 and 90% at pH 7.0. The fermentation rate was also higher at pH 7.6 than at pH 7.0. In batch fermentation of whey permeate containing about 5% lactose at pH 7.6, the concentration of acetic acid reached 20 g/l within 20 h. The production rate then became very slow due to end-product inhibition and high Na⁺ concentration. About 30 g/l acetate and 20 g/l lactate were obtained at a fermentation time of 80 h. However, when diluted whey permeate containing 2.5% lactose was used, all the whey lactose was converted to acetic acid within 30 h by this mixed culture.     

Partial characterization of anrpoD-like gene oflactoccocus lactis subsp.lactis ML3 with a polymerase chain reaction-based approach

With degenerated oligonucleotide primers for conserved regions of bacterial sigma factor proteins, a 117-bp internal DNA fragment of anrpoD-like gene ofLactoccocus lactis subsp.lactis ML3 was amplified by the polymerase chain reaction (PCR). The DNA sequence of this PCR product was determined by cycle sequencing, and the deduced amino acid sequence of this internal fragment showed an extensive homology with the known sigma factor sequences from six other microorganisms and present a 13-amino acid region corresponding to the typical RpoD box of primary sigma factors. This PCR product was used as a probe to specifically detect sigma homologs inPediococcus acidilactici, Leuconostoc lactis, Lactobacillus helveticus, Lactobacillus acidophilus, Enterococcus faecalis, Streptococcus thermophilus, andLactococcus lactis subsp.cremoris. These data are consistent with the existence of a high similarity between the primary sigma factors from diverse Gram-positive microorganisms.     

The kinetics of end-product inhibition of l-lactate production from xylose and glucose by Lactococcus lactis IO-1

Summary The relative contributions of lactate inhibition and the generation of sterile (undividing) cells to the low xylose utilisation rate of Lactococcus lactis IO-1 was investigated. The lactate inhibition constant of xylose grown cells was shown to be 9.3 times more than that of glucose grown cells. However, the sterile cell production rate and LDH inactivation rate of the xylose cultures were at least 10 times less than the glucose cultures. Thus, it is suggested that the slower substrate consumption rate in xylose medium is caused mainly by the large inhibition constant for the end product.