Optimization of gluconic acid synthesis by removing limitations and inhibitions

The optimization task was performed using the gluconic acid synthesis by the Acetobacter methanolicusMB 58 strain. The microorganisms were grown continuously on methanol as the growth substrate. After finishing the growth process by the deficiency of N and P, the gluconic acid synthesis was started by adding glucose. The synthesis process was performed continuously. The oxygen transfer rate depended on the gluconic acid concentration. During the growth process, the oxygen transfer rate reached a value of about 13 g O₂ · kg^?1 · h^?1using a 30-l glass fermenter equipped with a 6 blade stirrer and fully baffled. This rate declined to a value of between 2 and 5 g O₂ · kg^?1 · h^?1 in the presence of gluconic acid concentrations above 150 g gluconic acid · kg^?1medium. The yield (g gluconic acid · g^?1glucose) depended on the gluconic acid concentration and amounted to y = 0.7 in relation to 150 g gluconic acid · kg^?1medium and y = 0.8 in relation to 200 g · kg^?1medium, respectively. The fermenters were coupled with ultrafiltration moduls (Fa. ROMICON and Fa. SARTORIUS). The biomass concentrations amounted from 5 to 40 g dry mass kg^?1medium. The ultrafiltration modules retained the biomass within the fermentation system. A glucose solution (30 to 50 weight percent glucose) was continuously dosed into the fermenter. The retention time was chosen between 2 and 30 h. The gluconic acid synthesis rate reached values of up to 32 g gluconic acid · kg^?1 · h^?1. Within a range of up to 250 g gluconic acid · kg^?1medium, the acid concentration had no influence on the enzyme activity.     

Dinitrophenol influences the rate and yield of Acetobacter methanolicus during the growth on glucose

Acetobacter methanolicuswas grown on glucose in the presence of dinitrophenol (DNP) under carbon/energy-limited conditions. DNP affected both the growth yield and the growth rate (D_sh) at which the energy generation was shifted from a complete to an incomplete substrate oxidation by using the PQQ-linked glucose dehydrogenase. The more the growth yield was decreased, the higher both the DNP concentration and the growth rate became. At about 0.53 mM DNP, growth was completely stopped. D_sh decreased from 0.21h^?1in the absence of DNP to 0.175 h^?1and 0.075 h^?1in the presence of 0.2 mM and 0.4 mM DNP, respectively. The experimental data are discussed in terms of the limitations in the generation of energy and some stress situations which are exerted by the presence of the uncoupler.     

Oxidative capacity determines the growth rate with Acetobacter methanolicus

The cultivation of Acetobacter methanolicus on various substrates revealed that the respective maximum growth rates are obtained at an almost identical oxidative capacity of about 16 mmoles of oxygen g (biomass)^?1·h^?1 under conditions of energy generations by complete substrate oxidation. This is considered to be an indication that the energy production rate determined by the capacity of the respiratory chain limits the growth rate in this strain. However, with glucose and glycerol, for example, a further increase in the growth rate is observed accompanied by the generation of products (gluconic acid or dihydroxyacetone, respectively). The incomplete oxidation should play the role of an additional energy generation. The potential for this rate increase is looked for in a higher energy gain derived from reduction equivalents (PQQH₂) in this periplasmic oxidation step in relation to the cytoplasmic reduction equivalents.     

Möglichkeiten zur Steigerung der Schwermetallsorptionsleistung von Mikroorganismen

The sorption capacity of silver on different biological materials has been investigated depending on physico-chemical pretreatments. The maximum silver loading values measured were compared with the values obtained with nontreated biomasses. The results show an increase of the loading capacity up to a factor of 10 in case of the alkalitreated biomasses. When the biomasses are extracted before being used as adsorbent with a solvent mixture of chloroform/methanol in a ratio of 2:1 the efficiency of the silver adsorbing power can be increased. Beyond that, the ability to adsorb silver can also be influenced when microorganisms are used as biocatalysts in a product synthesis before they are used as adsorbents. A strain of Acetobacter methanolicus possesses 1.8 times higher affinity to silver when it is employed in a process of gluconic acid production before adsorption. Physico-chemical pretreatments influence not only the loading capacity of the biological material, but also the contacting time required for the establishment of the adsorption equilibrium can be considerable reduced.     

Production of cellulose from glucose by Acetobacter xylinum

Acetobacter xylinum 1FO 13693 was selected as the best cellulose-producing bacterium among 41 strains belonging to the genus Acetobacter and Agrobacterium. Cellulose was found to be produced at the liquid surface in static liquid cultivation. The rate of cellulose production depended proportionally on the surface-area of the culture medium and was unaffected by the depth and volume of the medium. The optimum pH for cellulose production was 4.0 to 6.0. Glucose, fructose and glycerol were preferred carbon sources for cellulose production. The yield of cellulose, relative to the glucose consumed, decreased with an increase in initial glucose concentration, and gluconic acid accumulated at a high initial glucose concentration. The decrease in cellulose yield could be due to some glucose being metabolized to gluconic acid. However, the accumulated gluconic acid did not affect cellulose production. The culture conditions of the bacterium for cellulose production were optimized. The maximum production rate of cellulose was 36 g/d·m², with a yield of 100% for added glucose under the optimal conditions.     

Organoheterotrophe Laugung resistenter Materialien

Leaching processes can be classified in chemolithotrophic and organoheterotrophic mechanisms. In the case of chemolithotrophic leaching sulphide minerals, elemental sulphur, ferrous iron and a number of different reduced metals will be oxidized in a solution containing sulphuric acid of bacterial and/or chemical origin. Organoheterotrophic leaching however is connected with the accumulation of microbial metabolites such as organic acids, proteins, peptides and polysaccharides, which are capable to disintegrate ores, minerals or industrial wastes through dissolution, formation of complexes or chelates. Whereas at the present time chemolithotrophic leaching processes are in operation in industrial scale for the winning of copper, uranium and some other special metals, organoheterotrophic processes, their problems and technical applications are still under study. Therefore problems of organoheterotrophic leaching of chemical high resistant materials such as phosphorus furnace slag and zircon from the Baltic shield have been investigated with regard to possible technical applications for the winning of rare earth elements (REE) and other precious metals. Using a strain of Acetobacter methanolicus which is able to accumulate large amounts of gluconic acid on the basis of glucose or glucose containing by-products, leaching effects up to 90% of REE could be realized in the case of phosphorus furnace slag and up to 45% in the case of zircon.     

The linear oxidation of formaldehyde to CO2 as the proper energy generating sequence for the assimilation of methanol in Acetobacter methanolicus MB58

Acetobacter methanolicus MB58 can grow on methanol. Since this substrate exhibits to be energy deficient there must be a chance to oxidize methanol to CO₂ merely for purpose of energy generation. For the assimilation of methanol the FBP variant of the RuMP pathway is used. Hence methanol can be oxidized cyclically via 6-phosphogluconate. Since Acetobacter methanolicus MB58 possesses all enzymes for a linear oxidation via formate the question arises which of both sequences is responsible for generation of the energy required. In order to clarify this the linear sequence was blocked by inhibiting the formate dehydrogenase with hypophosphite and by mutagenesis inducing mutants defective in formaldehyde or formate dehydrogenase. It has been shown that the linear dissimilatory sequence is indispensable for methylotrophic growth. Although the cyclic oxidation of formaldehyde to CO₂ has not been influenced by hypophosphite and with mutants both the wild type and the formaldehyde dehydrogenase defect mutants cannot grown on methanol. The cyclic oxidation of formaldehyde does not seem to be coupled to a sufficient energy generation, probably it operates only detoxifying and provides reducing equivalents for syntheses. The regulation between assimilation and dissimilation of formaldehyde in Acetobacter methanolicus MB58 is discussed.Abbreviations ATP Adenosine-5-triphosphate - DCPIP 2,6-dichlorphenolindophenol - DW dry weight - ETP electron transport phosphorylation - FBP fructose-1,6-bisphosphate - MNNG N-methyl-N-nitro-N-nitrosoguanidine - PMS phenazine methosulfate - RuMP ribulose monophosphate - Ru5P ribulose-5-phosphate - SDS sodiumdodecylsulphate - TCA tricarboxylic acid - TYB toluylene blue Dedicated to Prof. Dr. Dr. S. M. Rapoport on occasion of his 75th birthday     

Methanol-Assimilation durch ein acidophiles Bacterium der Gattung Acetobacter

Generally, methylotrophic bacteria grow optimally in a pH range between 6 and 7.2. The assimilation of methanol can take place via several pathways. Acetobacter methanolicus preiers an acidic pH range for growth, the pH optimum is about 4, and it uses the FBP variant for methanol assimilation. The latter is interesting from a regulatory point of view because phosphofructokinase disappears during growth on glucose, which is assimilated via the hexosemonophosphate pathway. Since Entner-Doudoroff enzymes and phosphoketolase are absent in A. `ethanolicus as well as in non-methylotrophic Acetobacter and Gluconobacter species phosphofructokinase becomes a key enzyme of the assimilation of methanol. Although A. methanolicus uses the hexulosephosphate pathway the growth yield on methanol is smaller than with other “hexulosephosphate pathway bacteria” e. g. with obligate methanol assimilating bacteria. At first sight it may appear that the acidic optimum pH is responsible for the smaller growth yield and the discrepancy between the experimental and predicted values. The relationship between the dependence on and the protection from, high external proton concentration on the one hand and the causes of the low growth yield on the other are discussed. Accordingly, A. methanolicus and another heterotrophic acidophiles seem to be acidoresistant above all, their machinery guaranteeing the protection from the high proton concentration is responsible for the acidophily and the low growth efficiency is caused by a simple respiratory chain.     

Effects of growth rate and oxygen tension on glucose dehydrogenase activity inAcinetobacter calcoaceticus LMD 79.41

The regulation of the synthesis of the quinoprotein glucose dehydrogenase (EC 1.1.99.17) has been studied inAcinetobacter calcoaceticus LMD 79.41, an organism able to oxidize glucose to gluconic acid, but unable to grow on both compounds. Glucose dehydrogenase was synthesized constitutively in both batch and carbon-limited chemostat cultures on a variety of substrates. In acetate-limited chemostat cultures glucose dehydrogenase levels and the glucose-oxidizing capacity of whole cells were dependent on the growth rate. They strongly increased at low growth rates at which the maintenance requirement of the cells had a pronounced effect on biomass yield. Cultures grown on a mixture of acetate and glucose in carbon and energy-limited chemostat cultures oxidized glucose quantitatively to gluconic acid. However, during oxygen-limited growth on this mixture glucose was not oxidized and only very low levels of glucose dehydrogenase were detected in cell-free extracts. After introduction of excess oxygen, however, cultures or washed cell suspensions almost instantaneously gained the capacity to oxidize glucose at a high rate, by an as yet unknown mechanism.     

Glucose as an energy donor in acetate growing Acinetobacter calcoaceticus

Since glucose can be oxidized but not assimilated by Acinetobacter calcoaceticus 69-V the question arose whether energy generated by glucose oxidation can help incorporate carbon from heterotrophic substrates and, if so, what the efficiency of ATP production is like. For this reason this species was grown in the chemostat on acetate. After having reached steady state conditions an increasing concentration of glucose was added. This led to an increase in the biomass level from about 0.4 g/g for growth on acetate alone to 0.6–0.65 g/g in the presence of glucose, independently of either the growth rate or the steepness of the glucose gradient used. This upper value approximates about the limit of the carbon conversion efficiency calculated for non-glycolytic substrates. Glucose was almost exclusively oxidized to gluconic acid, 2- and 5-ketogluconates, and pentose 5-phosphates were found only in traces. These results demonstrate that glucose functions as an additional energy source in Acinetobacter calcoaceticus 69-V. From the transient behaviour of biomass increase and the mixing proportion at which the maximum growth yield on acetate in the presence of glucose was obtained it followed that two mol of ATP must have been generated per mol of glucose oxidized. This property is discussed in terms of coupling glucose dehydrogenase with the respiratory chain.Abbreviations G _ox glucose oxidized to gluconic acid - G _t amount of glucose necessary for complete substitution of S _d - S _o inlet concentration of the limiting carbon substrate - S _a and S _d assimilated and dissimilated part respectively of the carbon substrate - PQQ pyrrolo-quinoline-quinone - V _ATP ^Ac ATP gain from complete oxidation to CO₂ of acetate (P/O=2) - V _ATP ^Glc ATP gain from oxidation of glucose to gluconic acid     

Influence of carbon sources on the viability and resuscitation of Acetobacter senegalensis during high-temperature gluconic acid fermentation

Much research has been conducted about different types of fermentation at high temperature, but only a few of them have studied cell viability changes during high-temperature fermentation. In this study, Acetobacter senegalensis, a thermo-tolerant strain, was used for gluconic acid production at 38 °C. The influences of different carbon sources and physicochemical conditions on cell viability and the resuscitation of viable but nonculturable (VBNC) cells formed during fermentation were studied. Based on the obtained results, A. senegalensis could oxidize 95 g l^− 1 glucose to gluconate at 38 °C (pH 5.5, yield 83%). However, despite the availability of carbon and nitrogen sources, the specific rates of glucose consumption (q_s) and gluconate production (q_p) reduced progressively. Interestingly, gradual q_s and q_p reduction coincided with gradual decrease in cellular dehydrogenase activity, cell envelope integrity, and cell culturability as well as with the formation of VBNC cells. Entry of cells into VBNC state during stationary phase partly stemmed from high fermentation temperature and long-term oxidation of glucose, because just about 48% of VBNC cells formed during stationary phase were resuscitated by supplementing the culture medium with an alternative favorite carbon source (low concentration of ethanol) and/or reducing incubation temperature to 30 °C. This indicates that ethanol, as a favorable carbon source, supports the repair of stressed cells. Since formation of VBNC cells is often inevitable during high-temperature fermentation, using an alternative carbon source together with changing physicochemical conditions may enable the resuscitation of VBNC cells and their use for several production cycles.

     

Isolation of auxotrophic mutants from acetobacter methanolicus MB 58

The lysine content of the biomass of the acidophilic facultatively methylotrophic bacterium Acetobacter methanolicus MB 58 was increased by genetic manipulations. A homoserine auxotroph, MB 58.196, and a threonine auxotroph, MB 58.195, were obtained from Acetobacter methanolicus MB 58 by N-methyl-N′-nitro-N-nitrosoguanidine treatment. Investigations of enzyme activities revealed that the homoserine auxotroph lacks homoserine dehydrogenase activity, and the threonine auxotroph lacks homoserine kinase activity. Concerning the lysine-producing ability, only the homoserine auxotrophic mutant accumulates lysine in the intracellular pool. The intracellular lysine content of this mutant was increased 40-fold. An excretion of amino acids into the medium was not detected. A homoserine resistant mutant, MB 58.196.10, isolated from MB 58.196 by UV-irradiation, was able to excrete lysine. About 95% of free lysine were found in the culture medium. Altogether, the free lysine concentration was increased 800-fold in comparison to the wild-type strain. By these genetic manipulations the total lysine concentration of MB 58.196 was increased to 2.7% and of MB 58.196.10 to 56% in comparison to the wild-type strain.     

Gluconic Acid Fermentation by Pullularia pullulans

During the study on the sugar metabolism of molds, several strains of Pullularia pullulans were found to produce large amounts of gluconic acid from glucose. Thirty seven strains of P. pullulans were then tested for their acid-producing abilities. Seven strains did not produce any amount of gluconic acid. However, all of the other strains were shown to be capable of producing this acid. The superior strains produced yiclds of gluconic acid as high as about 90%, based on glucose available, in shaking cultures at 30°C after 2 days. The yields were increased up to approximately 100% during later stages. In addition to high yields, gluconic acid was produced exclusively by these strains. Glutamic acid and inorganic ammonium salts, such as (NH₄)₂SO₄, NH₄Cl and (NH₄)₂HPO₄, were favorable nitrogen sources for acid production. In the case of (NH₄)₂SO₄, the optimum concentration was 0.05%. The addition of CaCO₃ was essential for gluconic acid production by P. pullulans and a 3% concentration of CaC0₃ appeared to be desirable for the maximum conversion to gluconic acid in a medium containing 10% glucose.     

Continous production of free gluconic acid by Gluconobacter suboxydans IFO 3290 immobilized by adsorption on ceramic honeycomb monolith: effect of reactor configuration on further oxidation of gluconic acid to keto-gluconic acid

Summary Gluconobacter suboxydans IFO 3290 was immobilized by adsorption on ceramic honeycomb monolith, and continuous production of free gluconic acid from 100 g/l glucose was carried out in one- and three-stage monolith reactors. Further oxidation of gluconic acid to keto-gluconic acid by the immobilized cells has been found to be more suppressed in the three-stage monolith reactor. This finding can be explained by the fact that, with the three-stage reactor, the opportunity to oxidize gluconic acid further was decreased because the residence time of the reaction mixture at glucose conversion above the threshold value was shorter.     

Continuous production of gluconic acid by immobilized Gluconobacter oxydans cell bioreactor

Summary Living Gluconobacter oxydans cells were attached on fibrous nylon carrier. Free gluconic acid was directly continuously produced in an aerated tubular immobilized-cell bioreactor for at least 6 months, with a volumetric productivity of at least 5 g/lh at 100 g/l substrate glucose and about 80 g/l product gluconic acid concentrations. The highest volumetric productivity in respect to glucose concentration was obtained with 175 g/l glucose, with about 120 g/l product gluconic acid level. With self-directing optimization procedure in respect to maximum product gluconic acid level, productivities as high as about 12–15 g/lh were obtained at relatively high substrate feed rate of 0.166 l/lh and relatively low aeration rate of 0.5 l/lmin. The highest glucose conversion of about 96% was obtained with a long residence time, at the lowest substrate feed rate used at a relatively low aeration rate, resulting however in a significant increase in ketogluconic acid production.     

Selection of glucose-assimilating variants ofAcinetobacter calcoaceticus LMD 79.41 in chemostat culture

Glucose metabolism has been studied in two strains ofAcinetobacter calcoaceticus. Strain LMD 82.3, was able to grow on glucose and possessed glucose dehydrogenase (EC 1.1.99.17). Glucose oxidation by whole cells was stimulated by PQQ, the prosthetic group of glucose dehydrogenase. PQQ not only increased the rate of glucose oxidation and gluconic acid production but also shortened the lag phase for growth on glucose. Strain LMD 79.41 also possessed glucose dehydrogenase but was unable to grow on glucose. Batch cultures and carbon-limited chemostat cultures growing on acetate in the presence of glucose oxidized the sugar to gluconic acid, which was not further metabolized. However, after prolonged cultivation on mixtures of acetate and glucose, carbon-limited chemostat cultures suddenly acquired the capacity to utilize gluconate. This phenomenon was accompanied by the appearance of gluconate kinase and a repression of isocitrate lyase synthesis. In contrast to the starter culture, cells from chemostats which had been fully adapted to gluconate utilization, were able to utilize glucose as a sole carbon and energy source in liquid and solid media.     

Absence of glucose-induced cAMP signaling in the Saccharomyces cerevisiae mutants cat1 and cat3 which are deficient in derepression of glucose-repressible proteins

Addition of glucose to derepressed cells of the yeast Saccharomyces cerevisiae induces a transient, specific cAMP signal. Intracellular acidification in these cells, as caused by addition of protonophores like 2,4-dinitrophenol (DNP) causes a large, lasting increase in the cAMP level. The effect of glucose and DNP was investigated in glucose-repressed wild type cells and in cells of two mutants which are deficient in derepression of glucose-repressible proteins, cat1 and cat3. Addition of glucose to cells of the cat3 mutant caused a transient increase in the cAMP level whereas cells of the cat1 mutant and in most cases also repressed wild type cells did not respond to glucose addition with a cAMP increase. The glucose-induced cAMP increase in cat3 cells and the cAMP increase occasionally present in repressed wild type cells however could be prevented completely by addition of a very low level of glucose in advance. In derepressed wild type cells this does not prevent the specific glucose-induced cAMP signal at all. These results indicate that repressed cells do not show a true glucose-induced cAMP signal. When DNP was added to glucose-repressed wild type cells or to cells of the cat1 and cat3 mutants no cAMP increase was observed. Addition of a very low level of glucose before the DNP restored the cAMP increase which points to lack of ATP as the cause for the absence of the DNP effect. These data show that intracellular acidification is able to enhance the cAMP level in repressed cells. The glucose-induced artefactual increase occasionally observed in repressed cells is probably caused by the fact that their low intracellular pH is only restored after the ATP level has increased to such an extent that it is no longer limiting for cAMP synthesis. It is unclear why the artefactual increases are not always observed. Measurement of glucose- and DNP-induced activation of trehalase confirmed the physiological validity of the changes observed in the cAMP level. Our results are consistent with the idea that the glucose-induced signaling pathway contains a glucose-repressible protein and that the protein is located before the point where intracellular acidification triggers activation of the pathway.Abbreviations CCCP carbonyl cyanide m-chlorophenylhydrazone - DNP 2,4-dinitrophenol - Mes 4-morpholineethanesulfonic acid     

Effects of cellular ATP depletion on glucose transport and insulin signaling in 3T3-L1 adipocytes

Glucosamine induced insulin resistance in 3T3-L1 adipocytes, which was associated with a 15% decrease in cellular ATP content. To study the role of ATP depletion in insulin resistance, we employed sodium azide (NaN3) and dinitrophenol (DNP), which affect mitochondrial oxidative phosphorylation, to achieve a similar 15% ATP depletion. Unlike glucosamine, NaN3 and DNP markedly increased basal glucose transport, and the increased basal glucose transport was associated with increased GLUT-1 content in the plasma membrane without changes in total GLUT-1 content. These agents, like glucosamine, did not affect the early insulin signaling that is implicated in insulin stimulation of glucose transport. In cells with a severe 40% ATP depletion, basal glucose transport was similarly elevated, and insulin-stimulated glucose transport was similar in cells with 15% ATP depletion. In these cells, however, early insulin signaling was severely diminished. These data suggest that cellular ATP depletion by glucosamine, NaN3, and DNP exerts differential effects on basal and insulin-stimulated glucose transport and that ATP depletion per se does not induce insulin resistance in 3T3-L1 adipocytes.     

Sul Controllo Della Glicolisi Nel Lievito

Abstract

On the control of carbohydrate utilization in yeast. — The results of a previous investigation showed that in higher plants the stimulating action of 2,4 dinitrophenol (DNP) on oxygen uptake and glycolysis is accompained by a fall of the level of reducing sugars, due to an increase of their respiratory utilization, and thus — according to every evidence — of the rate of hexose phosphate synthesis.

In the present work, the occurrence of a similar phenomenon in yeast (where the inhibiting effect of DNP on glucose uptake is not so much marked as in higher plant tissue) was investigated.

Here again DNP, at a 10^-4M concentration, induced a rapid decrease of the disaccaride trehalose and of glycogen, such as to account for the increased rate of respiration and of fermentation. The ratio between the contributions to CO₂ of Carbons 1 and respectively 6 of glucose was not significantly changed by DNP, which suggests that at least part of the DNP induced increase of glycolysis was mediated by the Embden Meyerhof pathway, and thus that a larger amount of fructose diphosphate was formed in the presence of the uncoupler.

In other experiments the effects of DNP on the dissimilation of C¹⁴ labeled glucose, glycerol and pyruvate to CO₂ and ethanol, and on the incorporation of the radioactive isotope into various fractions, 15 minutes after feeding the labeled substrates, was investigated. It was found that:

1) Glucose and glycerol uptake is not markedly inhibited by DNP at the concentration employed (^10–4M).

2) In the absence of DNP, a considerable portion of the radioactivity fed as glucose or glycerol and taken up by the yeast cells is recovered in the glycogen and trehalose fractions. (35% of the glucose, and 22% of the glycerol taken up). This is also observed for carbons 2 and 3, but not for carbon 1 of pyruvate. This indicates a reversibility of the glycolitic processes comprehended in the region between phospho-enol pyruvate andpolysac-carides; while the pyruvate kinase reaction appears to represent a sharp barrier at the « lower » end of glycolysis.

3) DNP almost completely inhibited the incorporation of C¹⁴ from glucose and glycerol into glycogen and trehalose, although it increased the rate of its dissimilation to CO₂ and ethanol. The total amount of glucose and glycerol transformed in the various metabolites (and thus — according to every evidence — phosphorylated) was somewhat lowered and proteins synthesis severely depressed. These effects are interpreted as due to the uncoupling action of DNP at the mitochondrial level, and to the consequent general decrease of the ATP and UTP levels required for protein and for polysaccharide synthesis.     

Stabilization of a proteolytically sensitive cytoplasmic recombinant protein during transition to downstream processing

The influence of aeration and glucose feeding on the stability of recombinant protein A in Escherichia coli during the transition period from a fed‐batch cultivation to downstream processing was studied. Neither interruption of the feeding under aerobic conditions nor anaerobic conditions in presence of glucose could stabilize protein A completely and the intracellular ATP pool did not decrease to less than 0.75–1 mM by this treatment. On the other hand, the absence of both oxygen and glucose resulted in a decrease of the ATP pool to less than 0.5 mM and almost complete stabilization of protein A. The decrease of ATP was more severe when sulfite was used instead of nitrogen gas to create anaerobic conditions in presence of glucose. This also resulted in nearly complete stabilization of protein A, which might be explained by an inhibiting effect of sodium sulfite on fermentation. Therefore, protein stabilization and decrease of the ATP pool were correlated in experiments in vivo. The concentrations of ADP and AMP increased during starvation and may also play a role in stabilization of the protein in vivo. ATP may be a limiting factor of proteolysis also during further steps of downstream processing. Its concentration decreases by 80–90% during harvesting and centrifugation of biomass and even further during disruption of cells. However, neither addition nor regeneration of ATP in cell disintegrate was enough to restore degradation of protein A, indicating that an additional factor limits proteolysis in vitro. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 62: 730–738, 1999.