Methanol metabolism byEubacterium limosum B2: Effects of pH and carbon dioxide on growth and organic acid production

Growth ofEubacterium limosum B2 on methanol-CO₂ was dependent upon the pH; optimum growth rates were obtained at pH 7.3–7.4. Carbon dioxide, a necessary cosubstrate for methylotrophic growth on methanol, was a determining factor for both growth and the nature of the organic acid produced. The coefficient of affinity for CO₂ was not affected by variations in pH if calculated relative to the concentration of hydrogen carbonate (16 mM). Similarly the conversion rate for methanol into acetic acid and butyric acid remained constant regardless of the level of pH with a fixed concentration of hydrogen carbonate. The metabolism ofE. limosum B2 grown on methanol-CO₂ was regulated by the HCO ₃ ^- concentration in the medium.     

Effects of various organic acid supplements on growth rates of Eubacterium limosum B2 on methanol

Summary During anaerobic growth on methanol, Eubacterium limosum B2 produces acetic and butyric acids as overflow metabolites, but can be induced to produce other organic acids. All organic acids (C₂–C₆) tested had a similar effect on growth, although the toxicity of each was different e.g. increasing inhibition by acids of increasing chain length. Inhibition was only observed above a threshold concentration related to the molecular size of the organic acids. At higher concentrations the degree of inhibition was a linear function of concentration. In a mathematical treatment of the data the inhibition constant (K _p) was shown to be proportionate to the threshold value (P _c) of each organic acid and accurately predicted the growth characteristics of Eubacterium limosum on methanol following the addition of organic acid supplements.     

Enrichment of homoacetogens converting H2/CO2 into acids and ethanol and simultaneous methane production

An anaerobic granular sludge was enriched to utilize H₂/CO₂ in a continuous gas-fed up-flow anaerobic sludge reactor by applying operating conditions expected to produce acetic acid, butyric acid, and ethanol. Three stages of fermentation were found: Stage I with acetic acid accumulation with the highest concentration of 35 mM along with a pH decrease from initial 6 to 4.5. In Stage II, H₂/CO₂ was replaced by 100% H₂ to induce solventogenesis, whereas butyric acid was produced with the highest concentration of 2.5 mM. At stage III with 10 µM tungsten (W) addition, iso-valeric acid, valeric acid, and caproic acid were produced at pH 4.5–5.0. In the batch tests inoculated with the enriched sludge taken from the bioreactor (day 70), however, methane production occurred at pH 6. Exogenous 15 mM acetate addition enhanced both the H₂ and CO₂ consumption rate compared to exogenous 10, 30, and 45 mM acetate by the enriched sludge. Exogenous acetate was failed to be converted to ethanol using H₂ as electron donor by the enriched acetogens.     

Growth and butyric acid production by Clostridium populeti

The growth of Clostridium populeti in 2% (w/v) glucose medium containing 0.2% (w/v) yeast extract was optimal with 10 mM NH₄Cl as the nitrogen source. Although the maximum specific growth rate (=0.32 h^-1) with 5 mM NH₄Cl was similar, the biomass yield was about 30% lower than that at the optimum. Either sodium sulphide or cysteine-HCl at an optimum concentration of 0.33 mM and 5.0 mM respectively, could serve as the sole sulphur source for growth. The growth rate was unaffected by initial glucose concentrations of up to 10% (w/v), but in the presence of 15% glucose it declined by about 35%. The molar yield of butyric acid (mol/mol glucose) declined from 0.70 in 1% (w/v) initial glucose medium to 0.39 in 10% glucose medium. In 5.7% initial glucose medium, butyric acid levels of 6.3 g/l were obtained (0.56 mol butyrate/mol glucose) after 72 h of incubation in 2.5 l batch cultures. A decrease of about 50% in the maximum specific growth rate of C. populeti was observed in the presence of an initial concentration of either 1.2 g/l of butyric acid or 18.9 g/l of acetic acid.This paper is issued as NRCC No. 29032     

Buffering as a means for increasing growth and butanol production byClostridium acetobutylicum

Summary The objective of this work was to optimize butanol formation in the acetone-butanol-ethanol (ABE) fermentation by examining the level of buffering as it affects the dissociation of butyric acid to the less toxic butyrate anion. Experiments were carried out in batch culture using chemically defined (P2) or complex media containing various buffering agents. These included salts of acetate, citrate, phosphate, nitrate, or bicarbonate, representing a range of pK _a values and buffering capacities. Growth in highly buffered medium was found to increase the stationary phase cell density, carbohydrate utilization, and the final butanol concentration. At higher levels of buffering, increased growth and elevated concentrations of butyric acid were required to initiate solventogenesis, suggesting the involvement of a critical threshold level of undissociated butyric acid.     

Influence of sulphur-containing compounds on the growth of Methanosarcina barkeri in a defined medium

Summary Optimal growth of Methanosarcina barkeri occurred in a defined medium containing methanol when 2.5–4 mM sodium sulphide was added giving a concentration of 0.04–0.06 mM dissolved sulphide (HS^–+S^2–. When the sulphide concentration was too low for optimal growth (e.g., 0.1 mM Na₂S added) the addition of the redox resin Serdoxit acted as a sulphide reservoir and caused a significant stimulation of growth. Furthermore it could be demonstrated that iron sulphide, zinc sulphide or L-methionine could also act as sulphur sources while the addition of sodium sulphate to sulphide-depleted media failed to restore growth. The amino acid L-cysteine (0.85 mM) stimulated growth but could not replace Na₂S.Under optimal cysteine-and sulphide concentrations the generation time of this strain was about 7–9 h during growth on methanol, giving a growth yield of about 0.14 g/g methanol consumed. Different M. barkeri strains were also able to grow under these conditions on acetate (30–50 h doubling time) without a significant lag-phase and with complete substrate consumption even though the inoculum was grown on methanol or H₂–CO₂. When methanol and acetate were present as a mixture in the medium both were used simultaneously.     

Anaerobic degradation of sorbic acid by sulfate-reducing and fermenting bacteria: pentanone-2 and isopentanone-2 as byproducts

Strictly anaerobic bacteria were enriched and isolated from freshwater sediment sources in the presence and absence of sulfate with sorbic acid as sole source of carbon and energy. Strain WoSo1, a Gram-negative vibrioid sulfate-reducing bacterium which was assigned to the species Desulfoarculus (formerly Desulfovibrio) baarsii oxidized sorbic acid completely to CO₂ with concomitant stoichiometric reduction of sulfate to sulfide. This strain also oxidized a wide variety of fatty acids and other organic compounds. A Gram-negative rod-shaped fermenting bacterium, strain AmSo1, fermented sorbic acid stoichiometrically to about equal amounts of acetate and butyrate. At concentrations higher than 10 mM, sorbic acid fermentation led to the production of pentanone-2 and isopentanone-2 (3-methyl-2-butanone) as byproducts. Strain AmSo1 fermented also crotonate and 3-hydroxybutyrate to acetate and butyrate, and hexoses to acetate, ethanol, hydrogen, and formate. The guanine-plus-cytosine content of the DNA was 41.8±1.0 mol%. Sorbic acid at concentrations higher than 5 mM inhibited growth of this strain while strain WoSo1 tolerated sorbic acid up to 10 mM concentration.     

Acetate metabolism inMethanosarcina barkeri

Methanosarcina barkeri was grown by acetate fermentation in complex medium (N₂ gas phase). The molar growth yield was 1.6–1.9 g cells/mol methane formed. Under these conditions 63–82% of the methane produced byMethanosarcina strains was derived from the methyl carbon of acetate, indicating that some methane was derived from other media components. Growth was not demonstrated in complex media lacking acetate or mineral acetate medium containing acetate but lacking H₂/CO₂, methanol, or trypticase and yeast extract. Acetate metabolism byM. barkeri strain MS was further exmined in mineral acetate medium containing H₂/CO₂ and/or methanol, but lacking cysteine. Under these conditions, more methane was derived from the methyl carbon of acetate than from the carboxyl carbon. Methanogenesis from the methyl group increased with increasing acetate concentration. The methyl carbon contributed up to 42% of the methane formed with H₂/CO₂ and up to 5% with methanol. Methanol stimulated the oxidation of the methyl group of acetate to CO₂. The average rates of methane formation from acetate were 1.3 nomol/min ·ml/culture (0.04mg² cell dry weight) in defined media (gas phase H₂/CO₂) and complex media (gas phase N₂). Acetate contributed up to 60% of cell carbon formed under the growth conditions examined. Similar quantities of cell carbon were derived from the methyl and carboxyl carbons of acetate, suggesting incorporation of this compound as a two-carbon unit. Incorporated acetate was not preferentially localized in lipid material, as 70% of the incorporated acetate was found in the wall and protein cell fractions. Acetate catabolism was stimulated by pregrowing of cultures in media containing acetate, while acetate anabolism was not influenced. The results are discussed in terms of the differences between the mechanisms of acetate catabolism and anabolism.Abbreviations CH₃-S-CoM methyl coenzyme M - TCA trichloroacetic acid - CoM coenzyme M (2-mercaptoethane sulfonic acid) - E^o standard potential change (pH 7) - F₄₂₀ Factor 420, a low redox electron carrier - G^o standard free energy change (pH 7) - kJ kilojoules (=0.24 kilocalories) - PBBW Weimer's phosphate-buffered basal medium - X unknown C₁ carrier     

Regulation of methanol oxidation and carbon dioxide fixation in Xanthobacter strain 25a grown in continuous culture

The regulation of C₁-metabolism in Xanthobacter strain 25a was studied during growth of the organism on acetate, formate and methanol in chemostat cultures. No activity of methanol dehydrogenase (MDH), formate dehydrogenase (FDS) or ribulose-1,5-bisphosphate carboxylase/oxygenase (RuBisC/O) could be detected in cells grown on acetate alone over a range of dilution rates tested. Addition of methanol or formate to the feed resulted in the immediate induction of MDH and FDH and complete utilization (D=0.10 h^-1) of acetate and the C ₁-substrates. The activities of these enzymes rapidly dropped at the higher growth rates, which suggests that their synthesis is further controlled via repression by heterotrophic substrates such as acetate. Synthesis of RuBisC/O already occurred at low methanol concentrations in the feed, resulting in additive growth yields on acetate/methanol mixtures. The energy generated in the oxidation of formate initially allowed an increased assimilation of acetate (and a decreased dissimilation), resulting in enhanced growth yields on the mixture. RuBisC/O activity could only be detected at the higher formate/acetate ratios in the feed. The data suggest that synthesis of RuBisC/O and CO₂ fixation via the Calvin cycle in Xanthobacter strain 25 a is controlled via a (de)repression mechanism, as is the case in other facultatively autotrophic bacteria. Autotrophic CO₂ fixation only occurs under conditions with a diminished supply of heterotrophic carbon sources and a sufficiently high availability of suitable energy sources. The latter point is further supported by the clearly more pronounced derepressing effect exerted by methanol compared to formate.Abbreviations FDH formate dehydrogenase - FBPase fructose-1,6-bisphosphatase - ICDH isocitrate dehydrogenase - MDH methanol dehydrogenase - PQQ pyrrolo quinoline quinone - PRK phosphoribulokinase - RuBisC/O ribulose-1,5-bisphosphate carboxylase/oxygenase - RuMP ribulose monophosphate - TCA tricarboxylic acid cycle     

One substrate,many fates: different ways of methanol utilization in the acetogen Acetobacterium woodii

Acetogenic bacteria such as Acetobacterium woodii use the Wood–Ljungdahl pathway (WLP) for fixation of CO₂ and energy conservation. This pathway enables conversion of diverse substrates to the main product of acetogenesis, acetate. Methyl group containing substrates such as methanol or methylated compounds, derived from pectin, are abundant in the environment and a source for CO₂. Methyl groups enter the WLP at the level of methyltetrahydrofolic acid (methyl-THF). For methyl transfer from methanol to THF a substrate-specific methyltransferase system is required. In this study, we used genetic methods to identify mtaBC2A (Awo_c22760-Awo_c22740) as the methanol-specific methyltransferase system of A. woodii. After methyl transfer, methyl-THF serves as carbon and/or electron source and the respiratory Rnf complex is required for redox homeostasis if methanol + CO₂ is the substrate. Resting cells fed with methanol + CO₂, indeed converted methanol to acetate in a 4:3 stoichiometry. When methanol was fed in combination with other electron sources such as H₂ + CO₂ or CO, methanol was converted Rnf-independently and the methyl group was condensed with CO to build acetate. When fed in combination with alternative electron sinks such as caffeate methanol was oxidized only and resulting electrons were used for non-acetogenic growth. These different pathways for the conversion of methyl-group containing substrates enable acetogens to adapt to various ecological niches and to syntrophic communities.     

Catalysis of an isotopic exchange between CO2 and the carboxyl group of acetate by Methanosarcina barkeri grown on acetate

Cell suspensions of Methanosarcina barkeri (strain Fusaro) grown on acetate were found to catalyze the formation of methane and CO₂ from acetate (30–40 nmol/min·mg protein) and an isotopic exchange between the carboxyl group of acetate and ¹⁴CO₂ (30–40 nmol/min·mg protein). An isotopic exchange between [¹⁴C]-formate and acetate was not observed. Cells grown on methanol mediated neither methane formation from acetate nor the exchange reactions. The data indicate that the isotopic exchange between CO₂ and the carboxyl group of acetate is a partial reaction of methanogenesis from acetate. Both reactions were completely inhibited by low concentrations of cyanide (20 M) or of hydrogen (0.5% in the gas phase). Methane formation from acetate was also completely inhibited by low concentrations of carbon monoxide (0.2% in the gas phase) whereas only significantly higher concentrations of CO had an effect on the exchange reaction. In the concentration range tested KCN, H₂ and CO had no effect on methane formation from methanol or from H₂ and CO₂; however, cyanide (20 M) also affected methane formation from CO. The results are discussed with respect to proposed mechanisms of methane and CO₂ formation from acetate.     

Accumulation of eicosapentaenoic acid in <Emphasis Type="Italic">Nannochloropsis</Emphasis> sp. in response to elevated CO<Subscript>2</Subscript> concentrations

To increase eicosapentaenoic acid (EPA, 20:5, n-3) content in the marine alga Nannochloropsis sp., the effect of CO₂ concentration during cultivation has been investigated. In a batch culture under normal atmospheric conditions (0.037% CO₂), the EPA content per cell increased during the first 1.5 days and then decreased immediately even though the cells were in an exponential growth phase. Increasing the CO₂ concentration to 0.3% and 2% over day 1.5 retained the EPA content at the higher concentration for another 1 and 2 days, respectively, suggesting that the EPA accumulation is enhanced by elevated concentrations of CO₂. EPA accumulation in response to elevated CO₂ concentrations was also observed during a later growth phase when CO₂ was introduced after the decrease of EPA content. The addition of CO₂ caused a slight decrease in the pH of the medium though this was not the cause of the observed EPA accumulation as addition of acidic buffer did not affect the EPA content. The maximum EPA production was obtained when 2% CO₂ was supplied 12 h prior to the end of the exponential growth. The total EPA production during 4-day cultivation was about twice that obtained with ambient air. These results suggest that the available CO₂ concentration affects the EPA content in Nannochloropsis sp.     

Acetic acid from H2 and CO2

Cell extracts of a nonsporeforming strictly anaerobic bacterium, Acetobacterium woodii produced acetate in N-tris(Hydroxymethyl)methyl-2-aminoethane sulfonic acid or phosphate buffers from hydrogen and carbon dioxide. The formation of acetate was not dependent on the presence of ATP in the reaction mixture; ADP also did not influence the acetate production. Since acetic acid is the main fermentation product during growth of A. woodii with H₂ and CO₂, ATP must be synthesized in the course of acetate formation. The possible sites of ATP synthesis are discussed.     

Effect of substrate loading on hydrogen production during anaerobic fermentation by Clostridium thermocellum 27405

We have investigated hydrogen (H₂) production by the cellulose-degrading anaerobic bacterium, Clostridium thermocellum. In the following experiments, batch-fermentations were carried out with cellobiose at three different substrate concentrations to observe the effects of carbon-limited or carbon-excess conditions on the carbon flow, H₂-production, and synthesis of other fermentation end products, such as ethanol and organic acids. Rates of cell growth were unaffected by different substrate concentrations. H₂, carbon dioxide (CO₂), acetate, and ethanol were the main products of fermentation. Other significant end products detected were formate and lactate. In cultures where cell growth was severely limited due to low initial substrate concentrations, hydrogen yields of 1 mol H₂/mol of glucose were obtained. In the cultures where growth ceased due to carbon depletion, lactate and formate represented a small fraction of the total end products produced, which consisted mainly of H₂, CO₂, acetate, and ethanol throughout growth. In cultures with high initial substrate concentrations, cellobiose consumption was incomplete and cell growth was limited by factors other than carbon availability. H₂-production continued even in stationary phase and H₂/CO₂ ratios were consistently greater than 1 with a maximum of 1.2 at the stationary phase. A maximum specific H₂ production rate of 14.6 mmol g dry cell⁻¹ h⁻¹ was observed. As cells entered stationary phase, extracellular pyruvate production was observed in high substrate concentration cultures and lactate became a major end product.     

Mixotrophic growth of two thermophilic Methanosarcina strains, Methanosarcina thermophila TM-1 and Methanosarcina sp. SO-2P, on methanol and hydrogen/carbon dioxide

Two thermophilic strains, Methanosarcina thermophila TM-1 and Methanosarcina sp. SO-2P, were capable of mixotrophic growth on methanol and H₂/CO₂. Activated carbon was, however, found to be necessary to support good growth. Both strains used hydrogen and methanol simultaneously. When methanol was depleted, hydrogen utilization continued and methane was further produced with concurrent cell growth. UV epifluorescence microscopy revealed that aggregates of both strains exhibited a bright red fluorescence besides the usual blue-green fluorescence.     

Variations in the energy metabolism of biotechnologically relevant heterofermentative lactic acid bacteria during growth on sugars and organic acids

Heterofermentative lactic acid bacteria (LAB) such as Leuconostoc, Oenococcus, and Lactobacillus strains ferment pentoses by the phosphoketolase pathway. The extra NAD(P)H, which is produced during growth on hexoses, is transferred to acetyl-CoA, yielding ethanol. Ethanol fermentation represents the limiting step in hexose fermentation, therefore, part of the extra NAD(P)H is used to produce erythritol and glycerol. Fructose, pyruvate, citrate, and O₂ can be used in addition as external electron acceptors for NAD(P)H reoxidation. Use of the external acceptors increases the growth rate of the bacteria. The bacteria are also able to ferment organic acids like malate, pyruvate, and citrate. Malolactic fermentation generates a proton potential by substrate transport. Pyruvate fermentation sustains growth by pyruvate disproportionation involving pyruvate dehydrogenase. Citrate is fermented in the presence of an additional electron donor to acetate and lactate. Thus, heterofermentative LAB are able to use a variety of unusual fermentation reactions in addition to classical heterofermentation. Most of the reactions are significant for food biotechnology/microbiology.     

Isolation and characterization of a new,methylotrophic, acidogenic anaerobe,the marburg strain

The cellular characteristics of a new methylotrophic, acidogenic, anaerobic bacterium that was first isolated from a sewage digestor in Marburg, Federal Republic of Germany, is described. The Marburg strain is a mesophilic, Gram-positive, nonmotile, pleomorphic rod that performs homoacetic, homobutyric, or heteroacidic fermentations. Cell morphology varies from single or paired straight rods to rudimentary branched rods, club-shaped cells, or oval refractile cells. Cell heat resistance correlated with the presence of a few refractile cells. Electron micrographs of thin sections revealed a thick monolayered cell wall and an atypical spore structure. The DNA base composition was 48.8±0.2 mol% guanosine plus cytosine. Growth required factors in yeast extract; methanol, H₂/CO₂, glucose, fructose, lactate, and pyruvate were fermented as energy sources. Corrinoid levels varied from 0.35±0.16 to 7.9±1.6 μg/mg cell dry weight when cells 0.1% yeast extract, N₂/CO₂, 100 mM methanol, and 50 mM Na acetate displayed a 20h doubling time, finalA ₅₄₀ of 0.9, butyric acid yield of 25 mM, and ≈stoichiometry of 3 mol butyrate formed per 10 mol methanol fermented. The nameButyribacterium (emend.)methylotrophicum sp. nov. is proposed for the Marburg strain.     

不同磷、硫及二氧化碳浓度对标志链带藻生长和碳水化合物积累的影响

【目的】为了研究不同磷、硫及二氧化碳浓度对标志链带藻(Desmodesmus insignis)生长与碳水化合物积累的影响,本实验以改良BG11培养基为基础,设计了8种不同初始K_2HPO_4浓度、8种不同初始MgSO_4浓度及4种二氧化碳浓度培养标志链带藻。【方法】采用干重法和苯酚-硫酸法分别测定其生物质浓度与总碳水化合物的含量。【结果】实验结果显示,在高磷浓度(0.460 mmol/L)下生物量达到最高为6.37 g/L,磷浓度为0.230 mmol/L (对照组)时总碳水化合物含量及单位体积产率达到最高,分别为45.40%(%干重)和0.20 g/(L·d)。不同初始MgSO_4浓度实验结果显示,高硫浓度有利于标志链带藻生长及碳水化合物的积累,生物量、总碳水化合物含量及单位体积产率分别在硫浓度为1.217 mmol/L、0.609 mmol/L和1.824 mmol/L时达到最高,分别为7.02 g/L、51.6%(%干重)及0.26 g/(L·d)。当二氧化碳浓度为3%(V/V)时,标志链带藻生物量、总碳水化合物含量及单位体积产率均达到最高,分别为6.81 g/L、44.03%和0.20 g/(L·d)。【结论】因此,磷浓度为0.230 mmol/L、硫浓度为1.824 mmol/L和二氧化碳浓度为3%时最有利于标志链带藻生长及碳水化合物的积累。     

Nutritional Requirements of Methanosarcina sp. Strain TM-1

Methanosarcina sp. strain TM-1, an acetotrophic, thermophilic methanogen isolated from an anaerobic sludge digestor, was originally reported to require an anaerobic sludge supernatant for growth. It was found that the sludge supernatant could be replaced with yeast extract (1 g/liter), 6 mM bicarbonate-30% CO₂, and trace metals, with a doubling time on methanol of 14 h. For growth on either methanol or acetate, yeast extract could be replaced with CaCl₂ · 2H₂O (13.6 μM minimum) and the vitamin p-aminobenzoic acid (PABA, ca. 3 nM minimum), with a doubling time on methanol of 8 to 9 h. Filter-sterilized folic acid at 0.3 μM could not replace PABA. The antimetabolite sulfanilamide (20 mM) inhibited growth of and methanogenesis by Methanosarcina sp. strain TM-1, and this inhibition was reversed by the addition of 0.3 μM PABA. When a defined medium buffered with 20 mM N,N-bis(2-hydroxyethyl)-2-aminoethanesulfonic acid was used, it was shown that Methanosarcina sp. strain TM-1 required 6 mM bicarbonate-30% CO₂ for optimal growth and methanogenesis from methanol. Cells growing on acetate were less dependent on bicarbonate-CO₂. When we used a defined medium in which the only organic compounds present were methanol or acetate, nitrilotriacetic acid (0.2 mM), and PABA, it was possible to limit batch cultures of Methanosarcina sp. strain TM-1 for nitrogen at NH₄⁺ concentrations at or below 2.0 mM, in marked contrast with Methanosarcina barkeri 227, which fixes dinitrogen when grown under NH₄⁺ limitation.     

Growth yields and the efficiency of oxidative phosphorylation of Paracoccus denitrificans during two- (carbon) substrate-limited growth

Paracoccus denitrificans was grown aerobically during two-(carbon)substrate-limitation on mannitol and methanol in chemostat cultures. Theoretical growth parameters were calculated based on the presence of 2 or 3 sites in the electron-transport chain of Paracoccus denitrificans. Experimental growth parameters determined during two-(carbon)substrate growth were conform to the presence of 3 sites of oxidative phosphorylation, while cells grown only on mannitol possessed 2 sites. The maximum growth yield on adenosine triphosphate (ATP), corrected for maintenance requirements, determined in chemostat experiments in which the methanol concentration is less than 2.11 times the mannitol concentration was 8.6 g of biomass. When the methanol concentration was more than 2.11 times the mannitol concentration the maximum growth yield on adenosine triphosphate decreased due to the more energy consuming process of CO₂-assimilation. Cells use methanol only as energy source to increase the amount of mannitol used for assimilation purposes. When the methanol concentration in chemostat experiments was more than 2.11 times the mannitol concentration, all mannitol was used for assimilation and excess energy derived from methanol was used for CO₂-assimilation via the ribulose-bisphosphate cycle. The synthesis of ribulosebisphosphate carboxylase was repressed when the methanol concentration in chemostat experiments was less than 2.11 times the mannitol concentration or when Paracoccus denitrificans was grown in batch culture on both methanol and mannitol. When in chemostat experiments the methanol concentration was more than 2.11 times the mannitol concentration ribulose-bisphosphate carboxylase activity could be demonstrated and CO₂-assimilation will occur. It is proposed that energy produced in excess activates or derepresses the synthesis of the necessary enzymes of the ribulose-bisphosphate cycle in Paracoccus denitrificans. Consequently growth on any substrate will be carbonas well as energy-limited. When methanol is present in the nutrient cells of Paracoccus denitrificans synthesize a CO-binding type of cytochrome c, which is essential for methanol oxidase activity.The reason for the increase in efficiency of oxidative phosphorylation from 2 to 3 sites is most probably the occurrence of this CO-binding type of cytochrome c in which presence electrons preferentially pass through the a-type cytochrome region of the electron-transport chain.Non Standard Abbreviations X prosthetic group of methanol dehydrogenase - q _substrate specific rate of consumption of substrate (mol/g biomass. h.) - Y _substrate, Y _substrate ^MAX are respectively the growth yield and the maximum growth yield corrected for maintenance requirements (g biomass/mol) - m _substrate maintenance requirement (mol substrate/g biomass) - specific growth rate (h^-1) - M [methanol]/[mannitol] ratio in the nutrient - N part of mannitol that is assimilated when M=o - R _m amount of methanol-equivalents that has the same energy content as 1 mannitol-equivalent - P/O _N , P/O _F , P/O _X is the amount of ATP produced during electron-transport of two electrons from respectively NADH+H⁺, FADH₂ and XH₂ to oxygen