Competition between the facultatively chemolithotrophic Thiobacillus A2, an obligately chemolithotrophic Thiobacillus and a heterotrophic spirillum for inorganic and organic substrates

Competition in a chemostat between the versatile Thiobacillus A2 and the specialized T. neapolitanus for thiosulfate as the sole growth-limiting substrate, led to dominance of the specialized over the versatile organism, at dilution rates 0.025 h^-1. Increasing concentrations of acetate or glycollate in the thiosulfate medium caused increased relative numbers of T. A2 in steady states at D=0.07 h^-1. Eventually, with 10–12 mmol of organic substrate per litre, complete dominance of T. A2 over T. neapolitanus occurred.Mixed cultures of T. A2 and a specialized spirillumshaped heterotroph, competing for acetate as sole growth-limiting substrate resulted in complete dominance of the heterotroph at dilution rates of 0.07 and 0.15 h^-1. In this case increasing concentrations of thiosulfate in the acetate medium, up to 10 mM, eventually led to the elimination of the heterotroph.These results have been interpreted as evidence that T. A2 was growing mixotrophically. As the concentration of the second substrate was raised, the number of T. A2 cells increased and as a result T. A2 consumed an increasing portion of the common substrate.In mixed chemostat cultures containing all three organisms, T. A2 could maintain itself with all tested ratios of acetate and thiosulfate in the inflowing medium. The heterotroph was excluded from the culture below a relatively low acetate to thiosulfate ratio, whilst above a relatively high acetate to thiosulfate ratio T. neapolitanus was completely eliminated.These results were discussed in relation to the ecological niche of Thiobacillus A2-type organisms.     

Regulation of autotrophic and heterotrophic metabolism in Pseudomonas oxalaticus OX1: Growth on mixtures of acetate and formate in continuous culture

Growth of Pseudomonas oxalaticus in carbon- and energy-limited continuous cultures with mixtures of acetate and formate resulted in the simultaneous utilization of both substrates at all dilution rates tested. During growth on these mixtures, acetate repressed the synthesis of ribulosebisphosphate carboxylase. The degree of this repression was dependent on the dilution rate and on the ratio of acetate and formate in the medium reservoir. At fixed acetate and formate concentrations in the inflowing medium of 30 and 100 mM, respectively, and dilution rates above 0.10h^-1, the severe repression of autotrophic enzymes resulted in a marked increase in bacterial dry weight compared to the growth yield of the organisms on the two substrates separately. Also, at these dilution rates a significant increase in isocitrate lyase activity was observed in the cells as compared to growth on acetate alone. This indicated that under these conditions more acetate was assimilated and less dissimilated since acetate was partly replaced by formate as the energy source. When formate was added to the reservoir of an acetate-limited culture (S_R=30 mM), derepression of RuBPCase synthesis was observed at formate concentrations of 50 mM and above. Below this concentration formate only served as an energy source for acetate assimilation; when its concentration was increased above 50 mM a progressively increasing contribution of carbon dioxide fixation to the total carbon assimilation was observed as the activity of RuBPCase in the cells increased. It is concluded that in Pseudomonas oxalaticus the synthesis of enzymes involved in autotrophic carbon dioxide fixation via the Calvin cycle is regulated by a repression/derepression mechanism.Abbreviations RuBPCase ribulosebisphosphate carboxylase - PMS phenazine methosulphate - DCPIP 2,6-dichlorophenol-indophenol - FDH formate dehydrogenase - S_R concentration of growth-limiting substrate in reservoir     

Mixed substrate growth of methylotrophic yeasts in chemostat culture: Influence of the dilution rate on the utilisation of a mixture of glucose and methanol

The growth of Hansenula polymorpha and Kloeckera sp. 2201 with a mixture of glucose and methanol (38.8%/61.2%, w/w) and the regulation of the methanol dissimilating enzymes alcohol oxidase, catalase, formaldehyde dehydrogenase and formate dehydrogenase were studied in chemostat culture, as a function of the dilution rate. Both organisms utilized and assimilated glucose and methanol simultaneously up to dilution rates of 0.30 h^-1 (H. polymorpha) and 0.26h^-1, respectively (Kloeckera sp. 2201) which significantly exceeded _max found for the two yeasts with methanol as the only source of carbon. At higher dilution rates methanol utilisation ceased and only glucose was assimilated. Over the whole range of mixed-substrate growth both carbon sources were assimilated with the same efficiency as during growth with glucose or methanol alone.In cultures of H. polymorpha, however, the growth yield for glucose was lowered by the unmetabolized methanol at high dilution rates. During growth on both carbon sources the repression of the synthesis of all catabolic methanol enzymes which is normally caused by glucose was overcome by the inductive effect of the simultaneously fed methanol. In both organisms the synthesis of alcohol oxidase was found to be regulated differently as compared to catalase, formaldehyde and formate dehydrogenase. Whereas increasing repression of the synthesis of alcohol oxidase was found with increasing dilution rates as indicated by gradually decreasing specific activities of this enzyme in cell-free extracts, the specific activities of this enzyme in cell-free extracts, the specific activities of catalase and the dehydrogenases increased with increasing growth rates until repression started. The results indicate similar patterns of the regulation of the synthesis of methanol dissimilating enzymes in different methylotrophic yeasts.Abbreviations and Terms C₁ Methanol - C₆ glucose; D dilution rate (h^-1) - D _c critical dilution rate (h^-1) - q _s specific, rate of substrate consumption (g substrate [g cell dry weight]^-1 h^-1) - q _CO2 and q _O2 are the specific rates of carbon dioxide release and oxygen consumption (mmol [g cell dry weight]^-1 h^-1) - RQ respiration quotient (q _CO2 q _O2 ¹ ) - s ₀(C₁) and s ₀(C₆) are the concentrations of methanol and glucose in the inflowing medium (g l^-1) - s residual substrate concentration in the culture liquid (g l^-1) - Sp. A. enzyme specific activity - x cell dry weight concentration (gl^-1) - Y _X/C6 growth yield on glucose (g cell dry weight [g substrate]^-1     

Benzene degradation by Ralstonia pickettii PKO1 in the presence of the alternative substrate succinate

The regulation of benzene degradation by Ralstonia pickettii PKO1 in the presence of the alternative substrate succinate was investigated in batch and continuous culture. In batch culture, R. pickettii PKO1 achieved a maximum specific growth rate with benzene of 0.18 h⁻¹, while succinate allowed much faster growth (μ_max = 0.5 h⁻¹). Under carbon excess conditions succinate repressed benzene consumption resulting in diauxic growth whereas under carbon-limited conditions in the chemostat both substrates were used simultaneously. Moreover, the effect of succinate on the adaptation towards growth with benzene was investigated in carbon-limited continuous culture at a dilution rate of 0.1 h⁻¹ by changing the inflowing carbon substrate from succinate to different mixtures of benzene and succinate. The adaptation process towards utilisation of benzene was rather complex. Three to seven hours after the medium shift biomass production from benzene started. Higher proportions of succinate in the mixture had a positive effect on both the onset of biomass production and on the time required for induction of benzene utilisation. Strikingly, after the initial increase in biomass and benzene-catabolising activities, the culture collapsed regularly and wash-out of biomass was observed. After a transient phase of low biomass concentrations growth on benzene resumed so that finally rather stable and high biomass concentrations were reached. The decrease in biomass and degradative activities cannot be explained so far, but the possibilities of either intoxication of the cells by benzene itself, or of inhibition by degradation intermediates were ruled out.     

Lipid accumulation in <Emphasis Type="Italic">Schizochytrium</Emphasis> G13/2S produced in continuous culture

Lipid and docosahexaenoic acid (DHA) accumulation into Schizochytrium G13/2S was studied under batch and continuous culture. Different glucose and glutamate concentrations were supplemented in a defined medium. During batch cultivation, lipid accumulation, 35% total fatty acids (TFA) occurred at the arithmetic growth phase but ceased when cell growth stopped. When continuous culture was performed under different glutamate concentrations, nitrogen-growth-limiting conditions induced the accumulation of 30–28% TFA in Schizochytrium. As the dilution rate decreased from 0.08 to 0.02 h⁻¹, both cell dry weight and TFA content of the cell increased. Under a constant dilution rate of 0.04 h⁻¹, carbon-limiting conditions decreased the TFA to 22%. Fatty acid profile was not affected by the different nutrient concentrations provided during continuous culture. Consequently, lipid accumulation can be induced through the carbon and nitrogen source concentration in the medium to maximise the TFA and subsequently DHA productivity by this microorganism.     

Oxidation of amines by yeasts grown on 1-aminoalkanes or putrescine as the sole source of carbon,nitrogen and energy

The maximum growth rate of Trichosporon cutaneum CBS 8111 in chemostat cultures was 0.185 h^-1 on ethylamine and 0.21 h^-1 on butylamine, that of Candida famata CBS 8109 was 0.32 h^-1 on putrescine.The amine oxidation pattern of the ascomycetous strains studied, viz. Candida famata CBS 8109, Stephanoascus ciferrii CBS 4856 and Trichosporon adeninovorans CBS 8244 was independent of the amine that had been used as the growth substrate. It resembled that of benzylamine/putrescine oxidase found in other ascomycetous yeasts. However, differences in pH optimum and substrate specificity were observed between the amine-oxidizing systems of these three species.The amine oxidation pattern of cell-free extracts of Trichosporon cutaneum CBS 8111 varied with the amine that was used as growth substrate. The enzyme system produced by Cryptococcus laurentii CBS 7140 failed to oxidize isobutylamine and benzylamine, and showed a high pH optimum.The synthesis of amine oxidase in the four yeast strains studied was not repressed by ammonium chloride and was weakly repressed by glucose but was strongly repressed if both compounds were present in the growth medium.     

Regulation of methylotrophic and heterotrophic metabolism in Arthrobacter P1. Growth on mixtures of methylamine and acetate in batch and continuous cultures

Incubations of Arthrobacter P1 in batch culture in media with mixtures of acetate and methylamine resulted in sequential utilization of the two carbon substrates, but not in diauxic growth. Irrespective of the way cells were pregrown, acetate was the preferred substrate and subsequent studies showed that this is due to the fact that acetate is a strong inhibitor of the methylamine transport system and amine oxidase in Arthrobacter P1. An analysis of enzyme activities in cell-free extracts showed that synthesis of amine oxidase occurred already in the first growth phase with acetate, whereas rapid synthesis of hexulose phosphate synthase was only observed once methylamine utilization started. It is therefore concluded that in Arthrobacter P1 the synthesis of the enzymes specific for methylamine oxidation is not regulated co-ordinately with those involved in formaldehyde fixation, but induced sequentially by methylamine and formaldehyde, respectively.During growth of Arthrobacter P1 on the same mixture in carbon- and energy source-limited continuous cultures both substrates were used simultaneously and completely at dilution rates below the _max on either of these substrates. Addition of methylamine, in concentrations as low as 0.5 mM, to the medium reservoir of an acetate-limited continuous culture (D=0.10 h^-1) already resulted in synthesis of both amine oxidase and hexulose phosphate synthase. In the reverse experiment, addition of acetate to the medium reservoir of a methylamine-limited continuous culture (D=0.10 h^-1), acetate was initially only used as an energy source. Synthesis of the glyoxylate cycle enzymes, however, did occur at acetate concentration in the feed above 7.5–10 mM. This indicates that at acetate concentrations below 10 mM the metabolism of the C₁ substrate methylamine is able to cause a complete repression of the synthesis of the enzymes involved in carbon assimilation from the C₂ substrate acetate.Abbreviations HPS Hexulose phosphate synthase - MS mineral salts - RuMP ribulose monophosphate     

Reduced inorganic sulfur oxidation supports autotrophic and mixotrophic growth of Magnetospirillum strain J10 and Magnetospirillum gryphiswaldense

Magnetotactic bacteria are present at the oxic–anoxic transition zone where opposing gradients of oxygen and reduced sulfur and iron exist. Growth of non‐magnetotactic lithoautotrophic Magnetospirillum strain J10 and its close relative magnetotactic Magnetospirillum gryphiswaldense was characterized in microaerobic continuous culture. Both strains were able to grow in mixotrophic (acetate + sulfide) and autotrophic (sulfide or thiosulfate) conditions. Autotrophically growing cells completely converted sulfide or thiosulfate to sulfate and produced 7.5 g dry weight per mol substrate at a maximum observed growth rate of 0.09 h^?1 for strain J10 and 0.07 h^?1 for M. gryphiswaldense. The respiratory activity for acetate was repressed in autotrophic and also in mixotrophic cultures, suggesting acetate was used as C‐source in the latter. We have estimated the proportions of substrate used for assimilatory processes and evaluated the biomass yields per mol dissimilated substrate. The yield for lithoheterotrophic growth using acetate as the C‐source was approximately twice the autotrophic growth yield and very similar to the heterotrophic yield, showing the importance of reduced sulfur compounds for growth. In the draft genome sequence of M. gryphiswaldense homologues of genes encoding a partial sulfur‐oxidizing (Sox) enzyme system and reverse dissimilatory sulfite reductase (Dsr) were identified, which may be involved in the oxidation of sulfide and thiosulfate. Magnetospirillum gryphiswaldense is the first freshwater magnetotactic species for which autotrophic growth is shown.     

Enhanced utilization-rate of methanol during growth on a mixed substrate: A continuous culture study with Hansenula polymorpha

The yeast Hansenula polymorpha was grown in a chemostat using either methanol or sorbitol as substrate or a mixture of both. Methanol alone could be utilized up to a dilution rate (D) of 0.18 h^-1, and sorbitol allowed growth at D's higher than 0.52 h^-1. In combination with sorbitol, methanol was completely utilized in the mixture even up to a D of 0.3 h^-1, and partially utilized at higher D's, To elucidate the basis of methanol utilization at high D's, enzyme activities on the single substrates and on the substrate mixture were compared. At D's above 0.3 h^-1 an increase of formate dehydrogenase activity was evident, an enzyme involved in the oxidation of methanol to carbon dioxide. It was concluded that at high D's large amounts of methanol were oxidized to generate energy. This was proved with ¹⁴C-methanol, and it was found that in the range of partial methanol utilization approximately 75% of methanol was converted to carbon dioxide and 25% incorporated into cell material.Abbreviation D dilution rate     

Enhanced continuous production of lovastatin using pellets and siran supported growth of Aspergillus terreus in an airlift reactor

Lovastatin, a hypocholesterolemic agent, is a secondary metabolite produced by filamentous microorganism Aspergillus terreus in submerged batch cultivation. Lovastatin production by pellets and immobilized siran cells was investigated in an airlift reactor. The process was carried out by submerged cultivation in continuous mode with the objective of increasing productivity using pellet and siran supported growth of A terreus. The continuous mode of fermentation improves the rate of lovastatin production. The effect of dilution rate and aeration rate were studied in continuous culture. The optimum dilution rate for pellet was 0.02 h⁻¹ and for siran carrier was 0.025 h⁻¹. Lovastatin productivity using immobilized siran carrier (0.0255 g/L/h) was found to be greater than pellets (0.022 g/L/h). The productivity by both modes of fermentation was found higher than that of batch process which suggests that continuous cultivation is a promising strategy for lovastatin production.     

An analysis of the growth of Gluconobacter oxydans in chemostat cultures

Gluconobacter oxydans was grown successively in glucose and nitrogen-limited chemostat cultures. Construction of mass balances of organisms growing at increasing dilution rates in glucose-limited cultures, at pH 5.5, revealed a major shift from extensive glucose metabolism via the pentose phosphate pathway to the direct pathway of glucose oxidation yielding gluconic acid. Thus, whereas carbon dioxide production from glucose accounted for 49.4% of the carbon input at a dilution rate (D)=0.05 h^-1, it accounted for only 1.3% at D=0.26 h^-1. This decline in pentose phosphate pathway activity resulted in decreasing molar growth yields on glucose. At dilution rates of 0.05 h^-1 and 0.26 h^-1 molar growth yields of 19.5 g/mol and 3.2 g/mol, respectively, were obtained. Increase of the steady state glucose concentration in nitrogen-limited chemostat cultures maintained at a constant dilution rate also resulted in a decreased flow of carbon through the pentose phosphate pathway. Above a threshold value of 15–20 mM glucose in the culture, pentose phosphate pathway activity almost completely inhibited. In G. oxydans the coupling between energy generation and growth was very inefficient; yield values obtained at various dilution rates varied between 0.8–3.4 g/cells synthesized per 0.5 mol of oxygen consumed.     

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.     

Optimization of culture conditions and continuous production of chitosan by the fungi,Absidia coerulea

The production of chitosan from the mycelia ofAbsidia coerulea was studied to improve cell growth and chitosan productivity. Culture conditions were optimized in batch cultivation (pH 4.5 agitator speed of 250 rpm, and aeration rate of, 2 vvm) and the maximum chitosan concentration achieved was 2.3 g/L under optimized conditions. Continuous culture was carried out successfully by the formation of new growth spots under optimized conditions, with a chitosan productivity of 0.052 gL⁻¹ h⁻¹, which is the highest value to date, and was obtained at a dilution rate of 0.05 h⁻¹. Cell chitosan concentrations reached about 14% in the steady state, which is similar to that achieved in batch culture. This study shows that for the continuous culture ofAbsidia coerulea it is vital to control the medium composition.     

Molar growth yields,respiration and cytochrome profiles of Beneckea natriegens when grown under carbon limitation in a chemostat

The effect of growth rate on the physiology of Beneckea natriegens was studied in chemostat culture. The molar growth yields (Y) from glucose and oxygen, the specific rates of oxygen (q _{O 2}) and glucose (q _glc) consumption and the specific rate of CO₂ production (q _{CO 2}) were linearly dependent on the growth rate over the dilution rate 0.17 h^-1 to 0.60 h^-1. Further increase in the dilution rate resulted in a decrease in growth yield and respiration rate and these changes were coincident with increases in the specific rate of glucose utilisation and of acetate production. The affinity of Beneckea natriegens for glucose was similar when measured either directly in chemostat culture or in a closed oxygen electrode system using harvested bacteria. The total content of cytochromes decreased with increasing growth rate. However, the quantity of CO-binding cytochromes remained independent of growth rate and correlated with the potential respiration rate.     

Effect of furfural on the growth of lactose-utilizing Candida Blankii 35

The effects of furfural on the growth of the lactose-utilizing yeast Candida blankii 35 were investigated using the method of continuous cultivation under conditions of carbon limitation and at dilution rates of 0.1 and 0.25 h⁻¹. The data obtained at dilution rate 0.1 h⁻¹ and 0.04% furfural showed a decrease in the yield of biomass by 6% and in the RNA content, but the synthesis of cell protein increased with 11.6% compared to the control. Treatment with 0.08% furfural induced significant changes in growth and biosynthesizing ability. A strong inhibitory effect of furfural was observed: the biomass yield decreased by half at 48 h and the culture the reached the control level of protein content. The effect of 0.02% furfural at 0.25 h⁻¹ dilution rate caused a significant reduction of biomass yield (34.4%) and the substrate utilization rate reached values higher by 52.4% at 48 h, but the protein-synthesizing ability of the cells slightly increased. The results showed that a treatment with 0.04 or 0.08% furfural caused significant disturbances of cell functions, the yields of biomass and protein drastically decreased and the culture was washed out. Data showed that the inhibitory effect of furfural on the growth and protein-synthesizing ability of Candida blankii 35 depends on the inhibitor concentration as well as the dilution rate. This revised version was published online in August 2006 with corrections to the Cover Date.     

Energetic aspects of anaerobic growth of Aerobacter aerogenes in complex medium

Molar growth yields for anaerobic growth of Aerobacter aerogenes in complex medium were much higher than for growth in minimal medium. In batch cultures the molar growth yield for glucose varied from 44 to 50 and Y _ATP from 17.1 to 18.8. For glucose-limited chemostat cultures a value of 17.5 g/mole was found for Y _ATP ^max and a value of 2.3 mmoles ATP/g dry weight h for the maintenance coeficient. Growth dependent pH changes were used to control the addition of fresh medium, containing excess of glucose to a continuous culture. The specific growth rate and the population density were dependent on the pH difference between the inflowing medium and the culture. At a value of 1.44 h^-1 the molar growth yield for glucose was about 70 and Y _ATP about 28.5. An-equation is presented, which gives the relation between theoretical and experimental Y _ATP ^max values.     

Chemostat culture of Bacillus caldotenax at 65°C: Activity and regulation of the main metabolic pathways

Bacillus caldotenax was cultivated in chemostat experiments at 65°C with a chemically defined minimal medium. Glycolysis, tricarboxylic acid cycle, pentose phosphate pathway and the respiratory chain were active as demonstrated by measuring the corresponding enzymes. No enzyme activity of the Entner-Doudoroff pathway could be detected. The specific activities of the citrate cycle enzymes were up to 10 times higher as compared to the enzymes of glycolysis. At dilution rates between 0.3 and 2.2 h^-1 none of the main metabolic pathways was regulated. In contrast the isocitrate lyase was regulated (drop of activity with increasing growth rates). As a result of a batch culture with glucose and acetate as carbon sources a regulation model was proposed: glucose, or a metabolite of glucose, represses the isocitrate lyase; in the absence of glucose acetate acts as an inducer.Abbreviations DCIP dichlorphenol indophenol - ED Entner-Doudoroff pathway - EMP Emden-Meyerhof-Parnas pathway - ICL isocitrate lyase - PP pentose phosphate pathway - TCC tricarbonic acid cycle     

Growth kinetics and Pho84 phosphate transporter activity of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> under phosphate-limited conditions

The effect of phosphate (P _i ) concentration on the growth behavior of Saccharomyces cerevisiae strain CEN.PK113-5D in phosphate-limited batch and chemostat cultures was studied. The range of dilution rates used in the present study was 0.08–0.45 h⁻¹. The batch growth of yeast cells followed Monod relationship, but growth of the cells in phosphate-limited chemostat showed change in growth kinetics with increasing dilution rates. The difference in growth kinetics of the yeast cells in phosphate-limited chemostat for dilution rates below and above approximately 0.2 h⁻¹ has been discussed in terms of the batch growth kinetic data and the change in the metabolic activity of the yeast cells. Immunological detection of a C-terminally myc epitope-tagged Pho84 fusion protein indicated derepressive expression of the Pho84 high-affinity P _i transporter in the entire range of dilution rates employed in this study. Phosphate transport activity mediated by Pho84 transporter was highest at very low dilution rates, i.e. 0.08–0.1 h⁻¹, corresponding to conditions in which the amount of synthesized Pho84 was at its maximum.     

Metabolism of lactose by Clostridium thermolacticum growing in continuous culture

The objective of the present study was to characterize the metabolism of Clostridium thermolacticum, a thermophilic anaerobic bacterium, growing continuously on lactose (10 g l⁻¹) and to determine the enzymes involved in the pathways leading to the formation of the fermentation products. Biomass and metabolites concentration were measured at steady-state for different dilution rates, from 0.013 to 0.19 h⁻¹. Acetate, ethanol, hydrogen and carbon dioxide were produced at all dilution rates, whereas lactate was detected only for dilution rates below 0.06 h⁻¹. The presence of several key enzymes involved in lactose metabolism, including beta-galactosidase, glyceraldehyde-3-phosphate dehydrogenase, pyruvate:ferredoxin oxidoreductase, acetate kinase, ethanol dehydrogenase and lactate dehydrogenase, was demonstrated. Finally, the intracellular level of NADH, NAD⁺, ATP and ADP was also measured for different dilution rates. The production of ethanol and lactate appeared to be linked with the re-oxidation of NADH produced during glycolysis, whereas hydrogen produced should come from reduced ferredoxin generated during pyruvate decarboxylation. To produce more hydrogen or more acetate from lactose, it thus appears that an efficient H₂ removal system should be used, based on a physical (membrane) or a biological approach, respectively, by cultivating C. thermolacticum with efficient H₂ scavenging and acetate producing microorganisms.     

Influence of culture conditions on the cell yield and amylases biosynthesis in continuous culture by Schwanniomyces castellii

Schwanniomyces castellii excreted -amylase and amyloglucosidase into the medium in the presence of starch. The biosynthesis and the rate of excretion were influenced by dissolved oxygen (specially for -amylase), pH of the culture and dilution rate. The cell yield observed (0.59) remained constant up to D=0.35h^-1 with starch as substrate. But in the case of growth on glucose, the yield observed was equal to 0.62 up to a dilution rate of D=0.18 h^-1. Beyond this value Y x/s decreased and ethanol was produced. The onset of fermentation dependend partly on the nature of the substrate and not only on the environment in particular on the quantity of dissolved oxygen present.