Experimental bioenergetics ofSaccharomyces cerevisiae in respiration and fermentation

Aerobic growth of Saccharomyces cerevisiae on glucose was investigated, focusing on the heat evolution as it relates to biomass and ethanol synthesis. “Aerobic fermentation” and “aerobic respiration” were established respectively in the experimental system by performing batch and fed-batch experiments. “Balanced growth” batch cultivations were carried out with initial sugar concentrations ranging from 10 to 70 g/L, resulting in different degrees of catabolite repression. The fermentative heat generation was continuously monitored in addition to the key culture parameters such as ethanol production rate, CO₂ evolution rate, O₂ uptake rate, specific growth rate, and sugar consumption rate. The respective variations of the above quantities reflecting the variations in the catabolic activity of the culture were studied. This was done in order to evaluate the microbial regulatory system, the energetics of microbial growth including the rate of heat evolution and the distribution of organic substrate between respiration and fermentation. This study was supported by closing C, energy, and electron balances on the system. The comparison of the fractions of substrate energy evolved as heat (δ_h) with the fraction of available electrons transferred to oxygen (?_O2) indicated equal values of the two (0.46) in the aerobic respiration (fed-batch cultivation). However, the glucose effect in batch cultivations resulted in smaller ?_O2 than δ_h, while both values decreased in their absolute values. The evaluation of the heat energetic yield coefficients, together with the fraction of the available electrons transferred to O, contributed to the estimation of the extent of heat production through oxidative phosphorylation.     

Characterization of a Corynebacterium Strain That Can Grow in Medium Containing up to 2 M Nitrate

A gram-positive bacterium, identified as Corynebacterium K37, was isolated from the waste effluent of a dairy farm. The bacterium thrived and expressed nitrate-reducing activity at nitrate concentrations of up to 2 M, and reduced nitrate concentration from 0.4 M to 11.4 mM and also from 0.4 M to 23.4 mM in aerobic and anaerobic fed-batch cultures, respectively. Cells of K37 were able to utilize a variety of carbon sources for nitrate reduction with little or no accumulation of nitrite. In aerobic cultures, the residual nitrite was minimal and it was completely reduced after prolonged incubation. Growth on acetate or pyruvate in anaerobic cultures resulted in lower nitrite reductase activities and concomitant higher residual nitrite concentrations than did growth on ethanol or glucose, suggesting that diminished electron availability was a factor in the accumulation of residual nitrite. The bacterium also survived in 2 M concentrations of NaCl, KCl, and CaCl₂. Corynebacterium sp. K37 may be useful in bioremediation of high nitrate pollution in contaminated soils and water.     

Isolation of hydrogen-producing bacteria from granular sludge of an upflow anaerobic sludge blanket reactor

H₂-producing bacteria were isolated from anaerobic granular sludge. Out of 72 colonies (36 grown under aerobic conditions and 36 under anaerobic conditions) arbitrarily chosen from the agar plate cultures of a suspended sludge, 34 colonies (15 under aerobic conditions and 19 under anaerobic conditions) produced H₂ under anaerobic conditions. Based on various biochemical tests and microscopic observations, they were classified into 13 groups and tentatively identified as follows: From aerobic isolates,Aeromonas spp. (7 strains),Pseudomonas spp. (3 strains), andVibrio spp. (5 strains); from anaerobic isolates,Actinomyces spp. (11 strains),Clostridium spp. (7 strains), andPorphyromonas sp. When glucose was used as the carbon substrate, all isolates showed a similar cell density and a H₂ production yield in the batch cultivations after 12h (2.24–2.74 OD at 600 nm and 1.02–1.22 mol H₂/mol glucose, respectively). The major fermentation by-products were ethanol and acetate for the aerobic isolates, and ethanol, acetate and propionate for the anaerobic isolates. This study demonstrated that several H₂ producers in an anaerobic granular sludge exist in large proportions and their performance in terms of H₂ production is quite similar.     

Physiological properties of Cellulomonas fermentans,a mesophilic cellulolytic bacterium

Summary The fermentation of cellobiose, glucose and cellulose MN 300 by Cellulomonas fermentans was studied. The molar growth yields (i.e. grams of cells per mole of hexose equivalent) were similar on cellobiose and cellulose at low sugar consumption levels (47.8 and 46.5 respectively), but was lower on glucose (38.0). The occurrence of cellobiose phosphorylase activity, detected in cellobiose- and cellulose-grown cells, might explain this result. The specific growth rates measured in cultures on cellobiose, glucose and cellulose were 0.055 h^-1, 0.040 h^-1 and 0.013 h^-1 respectively. Growth inhibition was observed, and a drop in Y_H occurred after relatively low but different quantities of hexose were consumed (2.2 mM, 5 mM and 8 mM hexose equivalent with cellulose, glucose and cellobiose respectively), which coincided with a change in the fermentative metabolism from a typical mixed acid metabolism (1 ethanol, 1 acetate and 2 formate synthesized by consumed hexose) to a more ethanolic fermentation. When growth ceased in cellulose cultures, consumption of cellulose continued, as did production of ethanol.Molar growth yields of C. fermentans were similar in anaerobic and aerobic cellobiose cultures (47.8 g/mol and 42.2 g/mol respectively). Specific growth rates were also quite similar under both culture conditions (0.055±0.013 h^-1 and 0.070±0.007 h^-1 respectively). Aerobic metabolism was studied using ¹⁴C glucose. During the exponential growth phase, acetate, succinate and nonidentified compound(s) accumulated in the supernatant, but no ¹⁴CO₂ was produced. During the stationary phase, acetate was oxidized and ¹⁴CO₂ produced, but without any further biomass synthesis. It seems that a blocking of metabolite oxidation may have occurred in C. fermentans except in the case of acetate, but acetate oxidation was apparently not coupled with production of energy utilizable in biosynthesis.     

Ester formation from ethanol by Candida pseudotropicalis

The production of ethanol, acetate ion and ethyl acetate from glucose by the yeast Candida pseudotropicalis NCYC 143 was investigated under aerobic and anaerobic growth conditions. Acetate and ethyl acetate only accumulated under aerobic conditions, whereas production of the alcohol was favoured by anaerobic conditions. Ester production during aerobic growth was enhanced substantially by growth in iron-deficient media. Possible conditions for optimising ester production from ethanol in dilute product streams were characterised.     

Thermophilic biohydrogen production by an anaerobic heat treated-hot spring culture

Batch experiments were conducted to investigate the thermophilic biohydrogen production using an enrichment culture from a Turkish hot spring. Following the enrichment, the culture was heat treated at 100 °C for 10 min to select for spore-forming bacteria. H₂ production was accompanied by production of acetate, butyrate, lactate and ethanol. H₂ production was associated by acetate–butyrate type fermentation while accumulation of lactate and ethanol negatively affected the H₂ yield. H₂ production was highest in the temperature range from 49.6 to 54.8 °C and optimum values for initial pH and concentrations of iron, yeast extract and glucose were 6.5, 40 mg/l, 4–13.5 g/l, respectively. PCR–DGGE profiling showed that the heat treated culture consisted of species closely affiliated to genus Thermoanaerobacterium.     

The impact of MIG1 and/or MIG2 disruption on aerobic metabolism of succinate dehydrogenase negative Saccharomyces cerevisiae

The zinc finger proteins Mig1 and Mig2 play important roles in glucose repression of Saccharomyces cerevisiae. To investigate whether the alleviation of glucose effect would result in an increase in aerobic succinate production, MIG1 and/or MIG2 were disrupted in a succinate dehydrogenase (SDH)-negative S. cerevisiae strain. Moreover, their impacts on physiology of the SDH-negative S. cerevisiae strain were studied under fully aerobic conditions when glucose was the sole carbon source. Our results showed that the succinate production for the SDH-negative S. cerevisiae was very low even under fully aerobic conditions. Furthermore, deletion of MIG1 and/or MIG2 did not result in an increase in succinate production in the SDH-negative S. cerevisiae strain. However, the synthesis of acetate was significantly affected by MIG1 deletion or in combination with MIG2 deletion. The acetate production for the mig1/mig2 double mutant BS2M was reduced by 69.72% compared to the parent strain B2S. In addition, the amount of ethanol produced by BS2M was slightly decreased. With the mig2 mutant BSM2, the concentrations of pyruvate and glycerol were increased by 26.23% and 15.28%, respectively, compared to the parent strain B2S.     

Metabolic control of Clostridium thermocellum via inhibition of hydrogenase activity and the glucose transport rate

Clostridium thermocellum has the ability to catabolize cellulosic biomass into ethanol, but acetic acid, lactic acid, carbon dioxide, and hydrogen gas (H₂) are also produced. The effect of hydrogenase inhibitors (H₂, carbon monoxide (CO), and methyl viologen) on product selectivity was investigated. The anticipated effect of these hydrogenase inhibitors was to decrease acetate production. However, shifts to ethanol and lactate production are also observed as a function of cultivation conditions. When the sparge gas of cellobiose-limited chemostat cultures was switched from N₂ to H₂, acetate declined, and ethanol production increased 350%. In resting cell suspensions, lactate increased when H₂ or CO was the inhibitor or when the cells were held at elevated hyperbaric pressure (6.8 atm). In contrast, methyl-viologen-treated resting cells produced twice as much ethanol as the other treatments. The relationship of chemostat physiology to methyl viologen inhibition was revealed by glucose transport experiments, in which methyl viologen decreased the rate of glucose transport by 90%. C. thermocellum produces NAD⁺ from NADH by H₂, lactate, and ethanol production. When the hydrogenases were inhibited, the latter two products increased. However, excess substrate availability causes fructose 1,6-diphosphate, the glycolytic intermediate that triggers lactate production, to increase. Compensatory ethanol production was observed when the chemostat fluid dilution rate or methyl viologen decreased substrate transport. This research highlights the complex effects of high concentrations of dissolved gases in fermentation, which are increasingly envisioned in microbial applications of H₂ production for the conversion of synthetic gases to chemicals.     

Fermentation and metabolic characteristics of Gluconacetobacter oboediens for different carbon sources

The metabolism of Gluconacetobacter oboediens was investigated in relation to different carbon sources for the continuous cultures at the dilution rate of 0.05 h⁻¹. The ¹³C-flux result implies the formation of metabolic recycles for the case of using glucose and acetate as carbon sources. When glucose and ethanol were used as carbon sources, the specific ethanol uptake rate and the specific acetate production rate increased as the feed ethanol concentration was increased from 40 to 60 g/l, while the specific CO₂ production rate and the biomass concentration decreased, where the ¹³C-metabolic flux result indicates that the glycolysis, oxidative PP pathway, and the tricarboxylic acid (TCA) cycle were less active, resulting in less biomass concentration. The flux result also implies that oxaloacetate decarboxylase flux became negative, so that oxaloacetate is backed up by this pathway, resulting in less activity of glyoxylate pathway. When gluconate was added for the case of using glucose and ethanol as carbon sources, the acetate and cell concentrations as well as gluconate concentrations increased. The glucose and ethanol concentrations decreased concomitantly with the increased feed gluconate concentration. In accordance with these fermentation characteristics, the enzyme activity result indicates that glucose dehydrogenase and glucose-6-phosphate dehydrogenase pathways became less active, while the glycolysis and the TCA cycle was activated as the feed gluconate concentration was increased.     

Analysis of metabolic pathways and fluxes in a newly discovered thermophilic and ethanol‐tolerant Geobacillus strain

A recently discovered thermophilic bacterium, Geobacillus thermoglucosidasius M10EXG, ferments a range of C5 (e.g., xylose) and C6 sugars (e.g., glucose) and is tolerant to high ethanol concentrations (10%, v/v). We have investigated the central metabolism of this bacterium using both in vitro enzyme assays and ¹³C‐based flux analysis to provide insights into the physiological properties of this extremophile and explore its metabolism for bio‐ethanol or other bioprocess applications. Our findings show that glucose metabolism in G. thermoglucosidasius M10EXG proceeds via glycolysis, the pentose phosphate pathway, and the TCA cycle; the Entner–Doudoroff pathway and transhydrogenase activity were not detected. Anaplerotic reactions (including the glyoxylate shunt, pyruvate carboxylase, and phosphoenolpyruvate carboxykinase) were active, but fluxes through those pathways could not be accurately determined using amino acid labeling. When growth conditions were switched from aerobic to micro‐aerobic conditions, fluxes (based on a normalized glucose uptake rate of 100 units (g DCW)^?1 h^?1) through the TCA cycle and oxidative pentose phosphate pathway were reduced from 64 ± 3 to 25 ± 2 and from 30 ± 2 to 19 ± 2, respectively. The carbon flux under micro‐aerobic growth was directed to ethanol, L ‐lactate (>99% optical purity), acetate, and formate. Under fully anerobic conditions, G. thermoglucosidasius M10EXG used a mixed acid fermentation process and exhibited a maximum ethanol yield of 0.38 ± 0.07 mol mol^?1 glucose. In silico flux balance modeling demonstrates that lactate and acetate production from G. thermoglucosidasius M10EXG reduces the maximum ethanol yield by approximately threefold, thus indicating that both pathways should be modified to maximize ethanol production. Biotechnol. Bioeng. 2009;102: 1377–1386. © 2008 Wiley Periodicals, Inc.     

Production of acetic acid by Acetogenium kivui

Summary The formation of acetic acid by the thermophilic nonsporeforming homoacetogenic bacterium Acetogenium kivui was studied under various conditions. In pH-controlled batch fermentation at pH 6.4 this bacterium was able to produce up to 625 mM of acetic acid from glucose within 50–60 h. The value of _max obtained was about 0.17 h^-1, the yield was about 2.55 mol of acetic acid per mol of glucose utilized. In continuous fermentation both substrate concentration and dilution rate (D) influenced the yield of acetate and the stationary concentration: a glucose concentration of 67 mM at D=0.09 h^-1 resulted in 2.82 mol acetate/mol glucose and 190 mM acetate at a production rate of 17.1 mM/1 h. When the dilution rate was increased the production rate reached a maximal value of 43.2 mM/1 h at D=0.32 h^-1. At a glucose concentration of 195 mM the dependence of yield upon dilution rate followed a similar pattern and an acetate concentration of 420 mM could be obtained. Enzymatic studies indicate that in A. kivui pyruvate ferredoxin-oxidoreductase and acetate kinase are inhibited at acetate concentrations higher than 800 mM. Based on these results a fed-batch fermentation was developed, which allowed to produce more than 700 mM acetic acid within 40–50 h.Dedicated to Prof. Dr. H. J. Rehm on the occasion of his 60th birthday     

Laboratory metabolic evolution improves acetate tolerance and growth on acetate of ethanologenic Escherichia coli under non-aerated conditions in glucose-mineral medium

In this work, Escherichia coli MG1655 was engineered to produce ethanol and evolved in a laboratory process to obtain an acetate tolerant strain called MS04 (E. coli MG1655: ΔpflB, ΔadhE, ΔfrdA, ΔxylFGH, ΔldhA, PpflB::pdc _Zm -adhB _Zm , evolved). The growth and ethanol production kinetics of strain MS04 were determined in mineral medium, mainly under non-aerated conditions, supplemented with glucose in the presence of different concentrations of sodium acetate at pH?7.0 and at different values of acid pH and a constant concentration of sodium acetate (2?g/l). Results revealed an increase in the specific growth rate, cell mass formation, and ethanol volumetric productivity at moderate concentrations of sodium acetate (2–10?g/l), in addition to a high tolerance to acetate because it was able to grow and produce a high yield of ethanol in the presence of up to 40?g/l of sodium acetate. Genomic analysis of the ΔpflB evolved strain identified that a chromosomal deletion of 27.3?kb generates the improved growth and acetate tolerance in MG1655 ΔpflB derivative strains. This deletion comprises genes related to the respiration of nitrate, repair of alkylated DNA and synthesis of the ompC gene coding for porin C, cytochromes C, thiamine, and colonic acid. Strain MS04 is advantageous for the production of ethanol from hemicellulosic hydrolysates that contain acetate.     

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.     

Enhancement of (R,R)-2,3-butanediol production from xylose by Paenibacillus polymyxa at elevated temperatures

Conversion of xylose to (R,R)-2,3-butanediol by Paenibacillus polymyxa in anaerobic batch and continuous cultures was increased by 39% and 52%, respectively, by increasing the growth temperatures from 30 to 39 °C. There was no effect of temperature when glucose was used as substrate. 39 mM (R,R)-2,3-butanediol, 65 mM ethanol, and 47 mM acetate were obtained from 100 mM xylose after 24 h batch culture at 39 °C. With 100 mM glucose and 100 mM xylose used together in a batch culture at 39 °C, all xylose was consumed after 24 h and 82 mM (R,R)-2,3-butanediol, 124 mM ethanol and 33 mM acetate were produced.     

Direct conversion of cellulose to methane by anaerobic fungus Neocallimastix frontalis and defined methanogens

Co-cultures of N. frontalis with a formate-utilizing methanogen, Methanobacterium formicicum and/or an aceticlastic methanogen, Methanosaeta concilii, were performed for methane production from cellulose. In the co-culture with M. formicicum, ca. 16 mM CH₄ was produced after 7 days without accumulation of H₂ and formate. In the co-culture with M. concilii, 12 mM CH₄ was produced after 17 days with decreasing acetate production. In the tri-culture of N. frontalis with M. formicicum and M. concilii, 24 mM CH₄ was produced after 17 days where acetate still remained at 23 mM, but production of lactate and ethanol decreased. When a 4-times concentrated culture broth of M. concilii was inoculated in this tri-culture system in a bioreactor, 150 mM CH₄ was produced after 24 days by feeding of cellulose, although 57 mM acetate still accumulated.     

Kinetics of biphasic growth of yeast in continuous and fed-batch cultures

The influence of dilution rate on the production of biomass, ethanol, and invertase in an aerobic culture of Saccharomyces carlsbergensis was studied in a glucose-limited chemostat culture. A kinetic model was developed to analyze the biphasic growth of yeast on both the glucose remaining and the ethanol produced in the culture. The model assumes a double effect where glucose regulates the flux of glucose catabolism (respiration and aerobic fermentation) and the ethanol utilization in yeast cells. The model could successfully demonstrate the experimental results of a chemostat culture featuring the monotonic decrease of biomass concentration with an increase of dilution rate higher than 0.2 hr^?1 as well as the maximum ethanol concentration at a particular dilution rate around 0.5 hr^?1. Some supplementary data were collected from an ethanol-limited aerobic chemostat culture and a glucose-limited anaerobic chemostat culture to use in the model calculation. Some parametric constants of cell growth, ethanol production, and invertase formation were determined in batch cultures under aerobic and anaerobic states as summarized in a table in comparison with the chemostat data. Using the constants, a prediction of the optimal control of a glucose fed-batch yeast culture was conducted in connection with an experiment for harvesting a high yield of yeast cells with high invertase activity.     

Investigation of the dark metabolism of acetate in photoheterotrophically grown cells ofRhodospirillum rubrum

The mechanism of the aerobic dark assimilation of acetate in the photoheterotrophically grown purple nonsulfur bacteriumRhodospirillum rubrum was studied. Both in the light and in the dark, acetate assimilation inRsp. rubrum cells, which lack the glyoxylate pathway, was accompanied by the excretion of glyoxylate into the growth medium. The assimilation of propionate was accompanied by the excretion of pyruvate. Acetate assimilation was found to be stimulated by bicarbonate, pyruvate, the C₄-dicarboxylic acids of the Krebs cycle, and glyoxylate, but not by propionate. These data implied that the citramalate (CM) cycle inRsp. rubrum cells can function as an anaplerotic pathway under aerobic dark conditions. This supposition was confirmed by respiration measurements. The respiration of cells oxidizing acetate depended on the presence of CO₂ in the medium. The fact that the intermediates of the CM cycle (citramalate and mesaconate) markedly inhibited acetate assimilation but had almost no effect on cell respiration indicated that citramalate and mesaconate were intermediates of the acetate assimilation pathway. The inhibition of acetate assimilation and cell respiration by itaconate was due to its inhibitory effect on propionyl-CoA carboxylase, an enzyme of the CM cycle. The addition of 5 mM itaconate to extracts ofRsp. rubrum cells inhibited the activity of this enzyme by 85%. The data obtained suggest that the CM cycle continues to function inRsp. rubrum cells that have been grown anaerobically in the light and then transferred to the dark and incubated aerobically.     

Growth and fermentation responses of Selenomonas ruminantium to limiting and non-limiting concentrations of ammonium chloride

 The objective of this study was to assess fermentation product, growth rate and growth yield responses of Selenomonas ruminantium HD₄ to limiting and non-limiting ammonia concentrations. The ammonia half-inhibition constant for S. ruminantium in batch culture was 296 mM. Cells were grown in continuous culture with a defined ascorbate-reduced basal medium containing either 0.5, 5, 25, 50, 100 or 200 mM NH₄Cl and dilution rates were 0.07, 0.14, 0.24 or 0.40 h^-1. Ammonia was the growth-limiting nutrient when 0.5 mM NH₄Cl was provided and the half-saturation constant was 72 μM. Specific rates of glucose utilization and fermentation acid carbon formation were highest for 0.5 mM NH₄Cl. Lactate production (moles per mole of glucose disappearing) increased at the fastest dilution rate (0.40 h^-1) for 5.0 mM NH₄Cl while acetate and propionate decreased when compared to slower dilutions (0.07 and 0.14 h^-1). Lactate production remained low while acetate and propionate remained high for all dilution rates when NH₄Cl concentrations were 25 mM or greater. Yield (Y _Glc and Y _ATP) were nearly doubled when NH₄Cl was increased from 0.5 mM (25.1 g cells/mol glucose used and 13.9 g cells/mol ATP produced respectively) to the higher concentrations. Y _Glc was highest at 25 mM and 50 mM NH₄Cl (48.2 cells/mol and 43.1 cells/mol respectively) as was Y _ATP (23.2 cells/mol and 20.8 cells/mol respectively). Y _NH3 was highest at the lowest NH₄Cl concentration. The maximal fermentation product formation rate occurred at a growth-limiting ammonia concentration, while maximal glucose and ATP bacterial yields occurred at non-growth-limiting ammonia concentrations. Given the growth response of this ruminal bacterium, it is possible that maximization of ruminal bacterial yield may necessitate sacrificing the substrate degradation rate and vice versa. Received: 5 December 1995/Received revision: 2 April 1996/Accepted: 22 April 1996     

Yeast mutants without phosphofructokinase activity can still perform glycolysis and alcoholic fermentation

Summary Mutants of Saccharomyces cerevisiae without detectable phosphofructokinase activity were isolated. They were partly recessive and belonged to two genes called PFK1 and PFK2. Mutants with a defect in only one of the two genes could not grow when they were transferred from a medium with a nonfermentable carbon source to a medium with glucose and antimycin A, an inhibitor of respiration. However, the same mutants could grow when antimycin A was added to such mutants after they had been adapted to the utilization of glucose. Double mutants with defects in both genes could not grow at all on glucose as the sole carbon source. Mutants with a single defect in gene PFK1 or PFK2 could form ethanol on a glucose medium. However, in contrast to wild-type cells, there was a lag period of about 2 h before ethanol could be formed after transfer from a medium with only nonfermentable carbon sources to a glucose medium. Wild-type cells under the same conditions started to produce ethanol immediately. Mutants with defects in both PFK genes could not form ethanol at all. Mutants without phosphoglucose isomerase or triosephosphate isomerase did not form ethanol either. Double mutants without phosphofructokinase and phosphoglucose isomerase accumulated large amounts of glucose-6-phosphate on a glucose medium. This suggested that the direct oxidation of glucose-6-phosphate could not provide a bypass around the phosphofructokinase reaction. On the other hand, the triosephosphate isomerase reaction was required for ethanol production. Experiments with uniformly labeled glucose and glucose labeled in positions 3 and 4 were used to determine the contribution of the different carbon atoms of glucose to the fermentative production of CO₂. With only fermentation operating, only carbon atoms 3 and 4 should contribute to CO₂ production. However, wild-type cells produced significant amounts of radioactivity from other carbon atoms and pfk mutants generated CO₂ almost equally well from all six carbon atoms of glucose. This suggested that phosphofructokinase is a dispensable enzyme in yeast glycolysis catalyzing only part of the glycolytic flux.     

Ethanol and acetate production by <Emphasis Type="Italic">Clostridium ljungdahlii</Emphasis> and <Emphasis Type="Italic">Clostridium autoethanogenum</Emphasis> using resting cells

Combined gasification and fermentation technologies can potentially produce biofuels from renewable biomass. Gasification generates synthesis gas consisting primarily of CO, CO₂, H₂, N₂, with smaller amounts of CH₄, NO_x, O₂, C₂ compounds, ash and tars. Several anaerobic bacteria species can ferment bottled mixtures of pure synthesis gas constituents. However, there are challenges to maintaining culture viability of synthesis gas exposed cells. This study was designed to enhance culture stability and improve ethanol-to-acetate ratios using resting (non-growing) cells in synthesis gas fermentation. Resting cell states were induced in autotrophic Clostridium ljungdahlii cultures with minimal ethanol and acetate production due to low metabolic activity compared to growing cell production levels of 5.2 and 40.1 mM of ethanol and acetate. Clostridium autoethanogenum cultures were not induced into true resting states but did show improvement in total ethanol production (from 5.1 mM in growing cultures to 9.4 in one nitrogen-limited medium) as well as increased shifts in ethanol-to-acetate production ratios.