Kinetics of product formation in batch and continuous culture of Clostridium barkeri

Summary The main fermentation end products in batch culture (unlimited glucose supply) of Clostridium barkeri were butyrate and lactate. The specific rate of butyrate production was linearly proportional to the growth rate while the specific rate of lactate production increased at low growth rates. In a glucose limited chemostat culture butyrate production was partly growth associated while acetate and lactate production was growth associated. Lactate was, however, only produced at high dilution rates. By varying the glucose concentration in the inflowing medium it was shown that lactate production was stimulated by a high feeding rate of the carbon source. These results are discussed in view of the fructose-1,6-diphosphate dependent lactate dehydrogenase activity in many other organisms.     

The regulation of carbohydrate metabolism in Klebsiella aerogenes NCTC 418 organisms,growing in chemostat culture

Klebsiella aerogenes NCTC 418 was grown in chemostat cultures (D=0.17 hr^-1; pH 6.8; 35° C) that were, successively, carbon-, sulphate-, ammonia-, and phosphate-limited, and which contained as the sole carbon-substrate first glucose, then glycerol, mannitol and lactate. Quantitative analyses of carbon-substrate used and products formed allowed carbon balances to be constructed and direct comparisons to be made of the effciency of substrate utilization. With all sixteen cultures, carbon recoveries of better than 90% were obtained.Optimum utilization of the carbon substrate was invariably found with the carbon-limited cultures, the sole products being organisms and carbon dioxide. But the extent to which excess substrate was over-utilized varied markedly with both the nature of the growth-limitation and the identity of the carbon-substrate. In general, sulphate-, ammonia-, and phosphate-limited cultures utilized glycerol more efficiently than mannitol, mannitol better than lactate, and glucose least efficiently. Glucose-containing cultures also synthesized some extracellular polysaccharide.When the carbon source was in excess, a range of acidic compounds generally were excreted. Sulphate-limited cultures, growing on glucose, excreted much pyruvate and acetate, whereas similarly-limited cultures growing on glycerol, mannitol or lactate produced only acetate. Ammonialimited cultures invariably excreted 2-oxoglutarate and acetate, whereas phosphate-limited cultures produced gluconic acid, 2-ketogluconic acid and acetate, when growing on glucose, but only acetate when growing on mannitol or lactate.From the rates of substrate and oxygen consumption, and the rates of cell synthesis, yield values for both substrate and oxygen were calculated. These showed different trends, but were similar in being highest under carbon-limitation and substantially lower under all other limitations.The physiological significance of these findings, and the probable nature of the regulatory mechanisms underlying overflow metabolism are discussed.     

Alternative schemes of butyrate production in Butyrivibrio fibrisolvens and their relationship to acetate utilization, lactate production, and phylogeny

Butyrivibrio fibrisolvens strains D1 and A38 produced little lactate, but strain 49 converted as much as 75% of its glucose to lactate. Strain 49 had tenfold more lactate dehydrogenase activity than strains D1 or A38, this activity was stimulated by fructose 1,6-bisphosphate, and had a pH optimum of 6.25. A role for fructose 1,6-bisphosphate or pH regulation of lactate production in strain 49 was, however, contradicted by the observations that very low concentrations (< 0.2 mM) of fructose 1,6-bisphosphate gave maximal activity, and continuous cultures did not produce additional lactate when the pH was decreased. The lactate production of strain 49 was clearly inhibited by the presence of acetate in the growth medium. When strain 49 was supplemented with as little as 5 mM acetate, lactate production decreased dramatically, and most of the glucose was converted to butyrate. Strain 49 did not possess butyrate kinase activity, but it had a butyryl-CoA/acetate CoA transferase that converted butyryl-CoA directly to butyrate, using acetate as an acceptor. The transferase had a low affinity for acetate (K _m of 5 mM), and this characteristic explained the acetate stimulation of growth and butyrate formation. Strains D1 and A38 had butyrate kinase but not butyryl-CoA/acetate CoA transferase, and it appeared that this difference could explain the lack of acetate stimulation and lactate production. Based on these results, it is unlikely that B. fibrisolvens would ever contribute significantly to the pool of ruminal lactate. Since relatives of strain 49 (strains Nor37, PI-7, VV1, and OB156, based on 16S rRNA sequence analysis) all had the same method of butyrate production, it appeared that butyryl-CoA/acetate CoA transferase might be a phylogenetic characteristic. We obtained a culture of strain B835 (NCDO 2398) that produced large amounts of lactate and had butyryl-CoA/acetate CoA transferase activity, but this strain had previously been grouped with strains A38 and D1 based on 16S rRNA sequence analysis. Our strain B835 had a 16S rRNA sequence unique from the one currently deposited in GenBank, and had high sequence similarity with strains 49 and Nor37 rather than with strains A38 or D1. Received: 3 December 1998 / Accepted: 18 February 1999     

Double mutation of the <Emphasis Type="Italic">PDC1</Emphasis> and <Emphasis Type="Italic">ADH1</Emphasis> genes improves lactate production in the yeast <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing the bovine lactate dehydrogenase gene

Expression of a heterologous l-lactate dehydrogenase (l-ldh) gene enables production of optically pure l-lactate by yeast Saccharomyces cerevisiae. However, the lactate yields with engineered yeasts are lower than those in the case of lactic acid bacteria because there is a strong tendency for ethanol to be competitively produced from pyruvate. To decrease the ethanol production and increase the lactate yield, inactivation of the genes that are involved in ethanol production from pyruvate is necessary. We conducted double disruption of the pyruvate decarboxylase 1 (PDC1) and alcohol dehydrogenase 1 (ADH1) genes in a S. cerevisiae strain by replacing them with the bovine l-ldh gene. The lactate yield was increased in the pdc1/adh1 double mutant compared with that in the single pdc1 mutant. The specific growth rate of the double mutant was decreased on glucose but not affected on ethanol or acetate compared with in the control strain. The aeration rate had a strong influence on the production rate and yield of lactate in this strain. The highest lactate yield of 0.75 g lactate produced per gram of glucose consumed was achieved at a lower aeration rate.     

An on-line technique for monitoring propionic acid fermentation

An on-line technique, based on measuring the increase in pressure due to CO₂ release in a closed air-tight reactor, was used to evaluate the fermentation of lactate by propionibacteria. The method was applied to batch cultures of Propionibacterium shermanii grown in yeast extract/sodium lactate medium containing lactate as a carbon source under micro-aerophilic conditions. Gas pressure evolution was compared both with substrate consumption and metabolites production and with acidification and growth. Linear relationships were found between gas pressure variation, lactate consumption and propionate and acetate production. The technique also enabled the evaluation of total CO₂ produced, by taking account of pressure, oxygen and pH measurements. These results tend to show that this simple and rapid method could be useful to monitor propionic acid bacteria growth.     

A kinetic model describing Shewanella oneidensis MR-1 growth, substrate consumption, and product secretion

Aerobic growth of Shewanella oneidensis MR-1 in minimal lactate medium was studied in batch cultivation. Acetate production was observed in the middle of the exponential growth phase and was enhanced when the dissolved oxygen (DO) concentration was low. Once the lactate was nearly exhausted, S. oneidensis MR-1 used the acetate produced during growth on lactate with a similar biomass yield as lactate. A two-substrate Monod model, with competitive and uncompetitive substrate inhibition, was devised to describe the dependence of biomass growth on lactate, acetate, and oxygen and the acetate growth inhibition across a broad range of concentrations. The parameters estimated for this model indicate interesting growth kinetics: lactate is converted to acetate stoichiometrically regardless of the DO concentration; cells grow well even at low DO levels, presumably due to a very low K(m) for oxygen; cells metabolize acetate (maximum specific growth rate, micro(max,A) of 0.28 h(-1)) as a single carbon source slower than they metabolize lactate (micro(max,L) of 0.47 h(-1)); and growth on acetate is self-inhibiting at a concentration greater than 10 mM. After estimating model parameters to describe growth and metabolism under six different nutrient conditions, the model was able to successfully estimate growth, oxygen and lactate consumption, and acetate production and consumption under entirely different growth conditions.     

Engineering Escherichia coli to improve culture performance and reduce formation of by-products during recombinant protein production under transient intermittent anaerobic conditions

Three E. coli strains, named VAL22, VAL23, and VAL24, were engineered at the level of mixed-acid fermentation pathways to improve culture performance under transient anaerobic conditions. VAL22 is a single mutant with an inactivated poxB gene that codes for pyruvate oxidase which converts pyruvate to acetate. VAL23 is a double mutant unable to produce lactate and formate due to deletions of the ldhA and pflB genes that code for lactate dehydrogenase and pyruvate-formate lyase, respectively. VAL24 is a triple mutant with ldhA and pflB deleted and poxB inactivated. Engineered strains were cultured under oscillating dissolved oxygen tension (DOT) in a scale-down system, to simulate gradients occurring in large-scale bioreactors. Kinetic and stoichiometric parameters of constant (10%) and oscillating DOT cultures of the engineered strains were compared with those of the parental strain, W3110. All strains expressed recombinant green fluorescent protein (GFP) as a protein model. Mutant strains showed improved specific growth rate, reduced by-product formation, and reduced specific glucose uptake rate compared to the parental strain, when cultured under oscillating DOT. In particular, lactate and formate production was abolished and acetate accumulation was reduced by 9-12%s. VAL24 showed the best performance, as specific growth and GFP production rates, and maximum GFP concentration were not affected by DOT gradients and were at least twofold higher than those of W3110 under constant DOT. Under oscillating DOT, VAL24 wasted about 40% less carbon into fermentation by-products than W3110. It was demonstrated that, although E. coli responds rapidly to DOT fluctuations by deviating to fermentative metabolism, such pathways can be eliminated as they are not necessary for bacterial survival during the short circulation times typical of large-scale cultures. The approach shown here opens new possibilities for designing metabolically engineered strains, with reduced sensitivity to DOT gradients and improved performance under typical conditions of large-scale cultures.     

The Influence of Carbon Source on the Products of Dissimilatory Iron Reduction

We have examined the influence of carbon source on both the rate of iron reduction and the mineralogy of the reduction products with Shewanella putrefaciens strain W3-18-1. When pyruvate was the carbon source, the secondary products were spherules composed of siderite. When uridine was used as the carbon source, the products were hexagonal plate-like structures identified as iron carbonate hydroxide hydrate, also known as carbonate green rust, a precursor to fougerite. When lactate was used as the carbon source, products were a mixture of iron carbonate hydroxide and magnetite. In terms of reaction stoichiometry, there were differences in the amount of acetate produced depending on the starting organic carbon source. Incubation with pyruvate produced a relatively large amount of acetate compared to incubation with uridine and lactate. There were also differences in the final pH of the cultures. While the pH for incubations with lactate started at 8.6 and ended between 8.0–8.3, the pH of cultures incubated with uridine was found to be almost a full unit lower at the conclusion of the experiment (～7.4). Solubility diagrams based on the chemistry found in our experiments predict that the production of Fe²⁺ _(aq) should always lead to the formation of magnetite. However, strain W3-18-1 produced different minerals depending on the carbon source utilized as the electron acceptor.     

Propionic acid fermentation by Propionibacterium acidipropionici: effect of growth substrate

Summary Batch propionic acid fermentations by Propionibacterium acidipropionici with lactose, glucose, and lactate as the carbon source were studied. In addition to propionic acid, acetic acid, succinic acid and CO₂ were also formed from lactose or glucose. However, succinic acid was not produced in a significant amount when lactate was the growth substrate. Compared to fermentations with lactose or glucose at the same pH, lactate gave a higher propionic acid yield, lower cell yield, and lower specific growth rate. The specific fermentation or propionic acid production rate from lactate was, however, higher than that from lactose. Since about equimolar acid products would be formed from lactate, the reactor pH remained relatively unchanged throughout the fermentation and would be easier to control when lactate was the growth substrate. Therefore, lactate would be a preferred substrate over lactose and glucose for propionic acid production using continuous, immobilized cell bioreactors. Correspondence to: S. T. Yang     

The kinetics of glucose fermentation bySelenomonas ruminantium HD4 grown in continuous culture

Summary The production of organic acids (acetate, lactate, and propionate) by the anaerobic, ruminal bacteriumSelenomonas ruminantium HD4 was investigated in both glucose-limited and glucose-sufficient (phosphate-limited) continuous cultures. The fermentation pattern of products exhibited a shift upon release of glucose limitation from acetate and propionate to lactate at a dilution rate of 0.2 h^–1. Glucose sufficiency brought about two-to fourfold increase in specific glucose utilization rate, lactate productivity, and lactate yield relative to glucose-limited growth conditions. The increased lactate production under glucose-sufficient growth conditions was attributed to the overutilization of excess glucose.The mention of firm names or trade products does not imply that they are endorsed or recommended by the U.S. Department of Agriculture over other firms or similar products not mentioned.     

The nature of the competitive ability of spontaneous staphylocoagulase-negative mutants of Staphylococcus aureus with respect to growth of the parent strains in continuous culture

During prolonged cultivation of S. aureus strains 104 and NCTC 8178 in continuous culture, staphylocoagulase-negative mutants arose and accumulated progressively in increasing proportions. The resulting loss of production of staphylocoagulase was accompanied by a simultaneous loss of production of -haemolysin and PV-leucocidin. Characterization of the strains revealed no further differences in biotype, exoenzymes, phage pattern and plasmid content.Cultivation in batch cultures showed that the maximal specific growth rates and specific oxygen-consumption rates of the mutant strains were slightly higher than those of the parent strains, whereas the production of total extracellular protein of the mutant strains had decreased significantly.From competition experiments between parent and mutant strains in chemostat cultures at different dilution rates and cultivation temperatures, it was concluded that the underlying mechanism of accumulation of staphylocoagulase-negative mutants in the chemostat is based on differences in affinity for the limiting substrate(s) rather than on differences in the production rates of total extracellular proteins. The complete repression of three exoenzymes, a partial repression of the total extracellular protein production, and an increased affinity for the limiting substrate(s) suggested that a mutation in a regulatory gene is involved. The possible role of a transposon in this mutation is discussed.     

Anaerobic Degradation of Lactate by Syntrophic Associations of Methanosarcina barkeri and Desulfovibrio Species and Effect of H(2) on Acetate Degradation

When grown in the absence of added sulfate, cocultures of Desulfovibrio desulfuricans or Desulfovibrio vulgaris with Methanobrevibacter smithii (Methanobacterium ruminantium), which uses H(2) and CO(2) for methanogenesis, degraded lactate, with the production of acetate and CH(4). When D. desulfuricans or D. vulgaris was grown in the absence of added sulfate in coculture with Methanosarcina barkeri (type strain), which uses both H(2)-CO(2) and acetate for methanogenesis, lactate was stoichiometrically degraded to CH(4) and presumably to CO(2). During the first 12 days of incubation of the D. desulfuricans-M. barkeri coculture, lactate was completely degraded, with almost stoichiometric production of acetate and CH(4). Later, acetate was degraded to CH(4) and presumably to CO(2). In experiments in which 20 mM acetate and 0 to 20 mM lactate were added to D. desulfuricans-M. barkeri cocultures, no detectable degradation of acetate occurred until the lactate was catabolized. The ultimate rate of acetate utilization for methanogenesis was greater for those cocultures receiving the highest levels of lactate. A small amount of H(2) was detected in cocultures which contained D. desulfuricans and M. barkeri until after all lactate was degraded. The addition of H(2), but not of lactate, to the growth medium inhibited acetate degradation by pure cultures of M. barkeri. Pure cultures of M. barkeri produced CH(4) from acetate at a rate equivalent to that observed for cocultures containing M. barkeri. Inocula of M. barkeri grown with H(2)-CO(2) as the methanogenic substrate produced CH(4) from acetate at a rate equivalent to that observed for acetate-grown inocula when grown in a rumen fluid-vitamin-based medium but not when grown in a yeast extract-based medium. The results suggest that H(2) produced by the Desulfovibrio species during growth with lactate inhibited acetate degradation by M. barkeri.     

Carbon and electron flow in Clostridium butyricum grown in chemostat culture on glucose-glycerol mixtures

Summary The metabolism of C. butyricum was manipulated, at neutral pH and in carbon limited chemostat cultures by changing the overall degree of reduction of the substrate, using mixtures of glucose and glycerol. Cultures grown on glucose alone produced only acids (acetate, butyrate and lactate). When the glycerol (in C moles)/glucose+glycerol (in C moles) ratio was progressively changed from 0 to 1 a corresponding increase of 1,3-propanediol production occured and an immediate and drastic decrease of the specific rate of acetate production was observed while the specific rate of butyrate production only decreased slightly. For glycerol (in C moles)/glucose+glycerol (in C moles) ratios higher than 0.5, the q_{NAD(P)H from Fd} and the CO₂/H₂ molar ratio increased sharply, the first becoming positive and the second higher than 1. This indicates a complete reversion of the electron flow: part of reduced ferredoxin produced by the phosphoroclastic cleavage of pyruvate to acetyl-CoA was diverted from H₂ formation toward NAD(P) reduction by the ferredoxin-NAD(P) reductase(s) in order to produce NAD(P)H. This change in the electron flow was associated to an increase in the specific rate and the yield of 1,3-propanediol production related to glycerol.     

Characterization of staphylococci isolated from mastitic cows in Spain.

A total of 57 gram-positive, catalase-positive cocci, considered etiological agents of clinical and subclinical bovine mastitis, were tested for glucose and mannitol fermentation, coagulase and thermonuclease production, sensitivity to lysostaphin, gelatin hydrolysis, lysozyme, phosphatase and egg yolk factor production, hemolytic properties, antibiotic sensitivity, susceptibility to human and bovine phages, and enterotoxin production. All 57 strains were identified as staphylococci. A good correlation was found between 3+ and 4+ coagulase reactions, thermonuclease production, and high sensitivity to lysostaphin. Neither mannitol fermentation nor production of other enzymes appeared to be a specific property of bovine Staphylococcus aureus strains. beta- and delta-hemolysins were more frequently found than alpha-hemolysin. Nearly 40% of the strains were penicillin resistant. Strains were lysed by phage 42E from the human phage set more frequently than by phage 42D, whereas with the bovine set, strains were more sensitive to specific bovine phages. Three strains produced enterotoxin C, and one strain produced enterotoxin D.     

Anaerobic fermentation of fructose in a mixed culture of fermentative and methanogenic bacteria

Summary Two newly isolated strains of Methanosarcina, strains JKAD and DALS, were grown in monoculture and in mixed culture in combination with Acetobacterium woodii WB1. Methanosarcina strains convert acetate into methane and carbon dioxide while Acetobacterium woodii grows on fructose, producing acetate via homoacetate fermentation. Monocultures of A. woodii in continuous culture consumed up to 6 mmoles g^-1 dry weight (dw) h^-1 of fructose and produced up to 12.9 mmoles g^-1 dw h^-1 of acetate at a dilution rate (D) of 0.13 h^-1. In batch growth the methanogenic bacteria produced up to 12.1 mmoles g^-1 dw h^-1 of CH₄ at a specific growth rate of 0.043 h^-1. In continuous cultivation the specific growth rate and the specific methane production of Methanosarcina were lower than in batch cultures, with values of 0.031 h^-1 and 3.1 mmoles g^-1 dw h^-1 of methane, respectively. In combination, A. woodii and Methanosarcina strain DALS in batch cultures completely converted fructose to methane and carbon dioxide with a maximum specific methane production rate of 1.9 mmoles g^-1 dw h^-1 of methane. In continuous cultivation these mixed cultures produced between 1.2 and 2 mmoles g^-1 dw h^-1 of CH₄ at a dilution rate of up to 0.043 h^-1. The methanogens were washed out at D values higher than 0.043 h^-1 for A. woodii and Methanosarcina strain JKAD, and higher than 0.05 h^-1 for A. woodii and Methanosarcina strain DALS. Data obtained from defined mixed cultures allow one to follow interactions in a mixed population of two species with different growth constants.     

Engineering Lactococcus lactis for production of mannitol: high yields from food-grade strains deficient in lactate dehydrogenase and the mannitol transport system

Mannitol is a sugar polyol claimed to have health-promoting properties. A mannitol-producing strain of Lactococcus lactis was obtained by disruption of two genes of the phosphoenolpyruvate (PEP)-mannitol phosphotransferase system (PTS(Mtl)). Genes mtlA and mtlF were independently deleted by double-crossover recombination in strain L. lactis FI9630 (a food-grade lactate dehydrogenase-deficient strain derived from MG1363), yielding two mutant (Delta ldh Delta mtlA and Delta ldh Delta mtlF) strains. The new strains, FI10091 and FI10089, respectively, do not possess any selection marker and are suitable for use in the food industry. The metabolism of glucose in nongrowing cell suspensions of the mutant strains was characterized by in vivo (13)C-nuclear magnetic resonance. The intermediate metabolite, mannitol-1-phosphate, accumulated intracellularly to high levels (up to 76 mM). Mannitol was a major end product, one-third of glucose being converted to this hexitol. The double mutants, in contrast to the parent strain, were unable to utilize mannitol even after glucose depletion, showing that mannitol was taken up exclusively by PEP-PTS(Mtl). Disruption of this system completely blocked mannitol transport in L. lactis, as intended. In addition to mannitol, approximately equimolar amounts of ethanol, 2,3-butanediol, and lactate were produced. A mixed-acid fermentation (formate, ethanol, and acetate) was also observed during growth under controlled conditions of pH and temperature, but mannitol production was low. The reasons for the alteration in the pattern of end products under nongrowing and growing conditions are discussed, and strategies to improve mannitol production during growth are proposed.     

Aerobic and anaerobic metabolism of Listeria monocytogenes in defined glucose medium.

A defined medium with glucose as the carbon source was used to quantitatively determine the metabolic end products produced by Listeria monocytogenes under aerobic and anaerobic conditions. Of 10 strains tested, all produced acetoin under aerobic conditions but not anaerobic conditions. Percent carbon recoveries of end products, typified by strain F5069, were as follows: lactate, 28%; acetate, 23%; and acetoin, 26% for aerobic growth and lactate, 79%; acetate, 2%; formate, 5.4%; ethanol, 7.8%; and carbon dioxide, 2.3% for anaerobic growth. No attempt to determine carbon dioxide under aerobic growth conditions was made. The possibility of using acetoin production to assay for growth of L. monocytogenes under defined conditions should be considered.     

GLUCOSE FERMENTATION AND GROWTH OF SELENOMONAS SPUTIGENA ON A MINIMAL MEDIUM

Very little is known about the growth physiology and metabolic niche of the human oral isolate Selenomonas sputigena. The objective of this study was to devise a minimal medium for comparing growth rates and fermentation of rumen Selenomonas ruminantium strains with S. sputigena. When anaerobically grown on a minimal glucose medium containing yeast extract as the only chemically undefined component, S. sputigena produced acetate, propionate, and succinate while S. ruminantium strains produced primarily lactate. When strains were compared (P < 0.05) for each carbon source that yielded growth, rumen strain HD₄ grew faster than all other strains on glucose, cellobiose and glycerol while strain GA192 grew faster on trehalose. Rumen strains GA192, PC18, and HD₄ grew faster on mannitol than rumen strains D and GA31. S. sputigena grew faster on lactate (0.38 ± 0.04) than any of the S. ruminantium strains. The minimal medium developed in this study should be useful for jurmer physiological studies on fermentation and metabolism in S. sputigena.     

Secretion of staphylocoagulase by Staphylococcus aureus: the role of a cell-bound intermediate

A cell-bound staphylocoagulase could be detected in chemostat cultures of Staphylococcus aureus 104 under magnesium- and oxygen-limited growth conditions. A distribution study revealed that 81% of the enzyme was membrane-bound and could be optimally released by Triton X-100. The remaining part was located in the periplasmic space and was released during protoplasting of the organism. From inhibition studies with cerulenin, quinacrine, lincomycin and chloramphenicol, it was concluded that the cell-bound form was a precursor in the secretion of extracellular staphylocoagulase. The involvement of a lipid intermediate/exoprotein- releasing protease system in the secretion of staphylocoagulase, and of exoproteins in general, is discussed.     

Lactate dehydrogenases in cyanobacteria

NAD-linked lactate dehydrogenases specific for the D- and L-lactate have been demonstrated in a number of strains of unicellular cyanobacteria. The D-lactate dehydrogenase of one strain (Synechococcus 6716) was partially purified and its properties were studied. The enzyme has a molecular weight of ca. 115000-120000, is highly specific, autooxidizable, and susceptible to inhibition by iodoacetamide, oxamate and ATP. The possible physiological functions of the enzyme in the metabolism of the organism were investigated. D-lactate carbon was incorporated in cell material during photosynthetic growth with CO2, but lactate was not used as sole source for carbon for photosynthetic or chemosynthetic development. D-lactate and pyruvate were oxidized aerobically in the dark by resting cell suspensions with the assimilation mainly of the C2 and the C3 carbon atoms. In the oxidation of lactate, acetate was excreted into the medium. No fermentation of glucose was found, but a small amount of D-lactate was detected as a product of endogenous dark metabolism of the cell. All enzymes required for the production of lactate from glucose and from glycogen were found in exponentially growing cells, but the activity of some key enzymes was low or undetectable in old cultures.