Carbon monoxide gasing leads to alcohol production and butyrate uptake without acetone formation in continuous cultures ofClostridium acetobutylicum

Summary When continuous, steady-state, glucose-limited cultures ofClostridium acetobutylicum were sparged with CO, the completely or almost completely acidogenic fermentations became solventogenic. Alcohol (butanol and ethanol) and lactate production at very high specific production rates were initiated and sustained without acetone, and little or no acetate and butyrate formation. In one fermentation, strong butyrate uptake without acetone formation was observed. Growth could be sustained even with 100% inhibition of H₂ formation. Although CO gasing inhibited growth up to 50%, and H₂ formation up to 100%, it enhanced the rate of glucose uptake up to 300%. TheY _ATP was strongly affected and mostly reduced with respect to its steady-state value. The results support the hypothesis that solvent formation is triggered by an altered electron flow.     

Energetics of glucose uptake in Salmonella typhimurium

We have studied the energetics of glucose uptake in Salmonella typhimurium. Strain PP418 transprots glucose via the phosphoenolpyruvate: glucose phosphotransferase system, while strain PP1705 lacks this system and can only use the galactose permease for glucose uptake. These two strains were cultured anaerobically in glucose-limited chemostats. Both strains produced ethanol and acetate in equimolar amounts but a significant difference was observed in the molar growth yield on glucose (Y _Glc). It is suggested that this difference is due to a difference in the energetics of the glucose uptake systems in the two strains.Assuming an equal Y _ATP for both strains, we could calculate that uptake of 1 mole of glucose via the galactose permease consumes the equivalent of 0.5 mole of ATP. With the additional assumption that one proton is transported in symport with one glucose molecule, these results imply a stoichiometry of two protons per ATP hydrolysed.Abbreviations PTS Phosphoenolpyruvate: carbohydrate phosphotransferase system - D dilution rate (h^-1 - DW dry weight - GalP galactose permease - EtOH ethanol - HAc acetate - Lact lactate - Suc succinate - HFo formate - Glc Glucose - Y _Glc, Y _ATP yield of cells per glucose or ATP - q specific production rate     

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.     

Continuous and biomass recycle fermentations of Clostridium acetobutylicum

Using experimental data from continuous cultures of Clostridium acetobutylicum with and without biomass recycle, relationships between product formation, growth and energetic parameters were explored, developed and tested. For glucose-limited cultures the maintenance models for, the Y _ATP and biomass yield on glucose, and were found valid, as well as the following relationships between the butanol (Y _B/G) or butyrate (Y _BE/G) yields and the ATP ratio (R _ATP, an energetic parameter), Y _B/G =0.82-1.35 R _ATP, Y _BE/G =0.54 + 1.90 R _ATP. For non-glucose-limited cultures the following correlations were developed, Y _B/G =0.57-1.07 , Y _B/G =0.82-1.35 R _ATPATP and similar equations for the ethanol yield. All these expressions are valid with and without biomass recycle, and independently of glucose feed or residual concentrations, biomass and product concentrations. The practical significance of these expressions is also discussed.List of Symbols D h^–1 dilution rate - m _e mol g^–1 h^–1 maintenance energy coefficient - m _G mol g^–1 h^–1 maintenance energy coefficient - R biomass recycle ratio, (dimensionless) - R _ATP ATP ratio (eqs.(5), (10) and (11)), (dimensionless) - X kg/m³ biomass concentration - Y _ATP g biomass per mol ATP biomass yield on ATP - Y _ATP ^max g biomass per mol ATP maximum Y _ATP - Y _A/G mol acetate produced per mol glucose consumed molar yield of acetate - y _an/g mol acetone produced per mol glucose consumed molar yield of acetone - Y _B/G mol butanol produced per mol glucose consumed molar yield of butanol - y _be/g mol butyrate produced per mol glucose consumed molar yield of butyrate - Y _E/G mol ethanol produced per mol glucose consumed molar yield of ethanol - Y _X/G g biomass per mol glucose consumed biomass yield on glucose - Y _ATP ^max g biomass per mol maximum Y _X/G glucose consumed - h^–1 specific growth rate     

A continuous culture study of an ATPase-negative mutant of Escherichia coli

For anaerobic glucose-limited chemostat cultures of Escherichia coli a value of 8.5 was found for Y _ATP ^max . For anaerobic glucose- or ammoniumlimited chemostat cultures of the ATPase-negative mutant M2-6 of E. coli Y _ATP ^max values of 17.6 and 20.0 were found, respectively. From these data it can be concluded that in the wild type during anaerobic growth 51–58% of the total ATP production is used for energetization of the membrane. Using the Y _ATP values obtained in the anaerobic experiments a P/O ratio of 1.46 could be calculated for aerobic experiments with the wild type. It is concluded that from the energy obtained by respiration in wild type E. coli about 60% is used for membrane energetization and only about 40% for the actual formation of ATP. No dramatic difference in the maintenance requirement for ATP or glucose has been observed between glucose- and ammonium-limited chemostat cultures of the mutant. The large difference in maintenance requirement observed for such cultures of the wild type is therefore supposed to be made possible by ATP hydrolysis by the ATPase.     

Glucose Fermentation by <Emphasis Type="Italic">Propionibacterium microaerophilum</Emphasis>: Effect of pH on Metabolism and Bioenergetic

pH affected significantly the growth and the glucose fermentation pattern of Propionibacterium microaerophilum. In neutral conditions (pH 6.5–7.5), growth and glucose fermentation rate (qs) were optimum producing propionate, acetate, CO₂, and formate [which together represented 90% (wt/wt) of the end products], and lactate representing only 10% (wt/wt) of the end products. In acidic conditions, propionate, acetate, and CO₂ represented nearly 100% (wt/wt) of the fermentation end products, whereas in alkaline conditions, a shift of glucose catabolism toward formate and lactate was observed, lactate representing 50% (wt/wt) of the fermentation end products. The energy cellular yields (Y _X/ATP), calculated (i) by taking into account extra ATP synthesized through the reduction of fumarate into succinate, was 6.1–7.2 g mol⁻¹. When this extra ATP was omitted, it was 11.9–13.1 g mol⁻¹. The comparison of these values with those of Y _X/ATP in P. acidipropionici and other anaerobic bacteria suggested that P. microaerophilum could not synthesize ATP through the reduction of fumarate into succinate and therefore differed metabolically from P. acidipropionici. Received: 8 April 2002 / Accepted: 8 May 2002     

Glucose fermentation byClostridium butyricum grown under a self generated gas atmosphere in chemostat culture

Summary Clostridium butyricum was grown anae-robically under glucose-limited conditions in che-mostat cultures under self generated gas atmo-sphere. It is shown that the quantitative composi-tion of the fermentation products is dependent on the pH value, the growth rate, the concentration of glucose in the growth medium and the compo-sition of the gas atmosphere developed in the reactor. The ratio q_acetate/q_butyrate increases from 0.06 to 0.66 in parallel with an increase in growth rate from 0.02 h⁻¹ to 0.29 h⁻¹ (at pH = 6.0). De-creasing the partial pressure of H₂ results in an in-crease of the q_acetate/q_butyrate ratio. The partial pressure of CO₂ in the reactor does not influence the fermentation products whatsoever. Increasing pH values (>6.8) and concentrations of glucose in the growth medium also result in increasing q_acetate/q_butyrate ratios. The maximal Y_ATP is con-stant from pH 4.8–6.0. The functioning of NADH₂-ferredoxin oxi-doreductase is discussed.     

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     

Energetics of Saccharomyces cerevisiae CBS 426: Comparison of anaerobic and aerobic glucose limitation

Saccharomyces cerevisiae CBS 426 was grown aerobically and anaerobically in a glucose-limited chemostat. The flows of biomass, glucose, ethanol, carbon dioxide, oxygen, glycerol, and the elemental composition of the biomass were measured. Models for anaerobic and aerobic growth are constructed. Values for Y_ATP and P/O are obtained from continuous culture data for aerobic growth; this Y_ATP value is compared with that obtained from the anaerobic growth results. The ratio between the heat produced and the oxygen consumed increases if more glucose in fermented to ethanol and carbon dioxide. An equation for ?_H/?_O as a function of the respiratory quotient is given.     

Effects of Acetate and Butyrate During Glycerol Fermentation by Clostridium butyricum

The effects of acetate and butyrate during glycerol fermentation to 1,3-propanediol at pH 7.0 by Clostridium butyricum CNCM 1211 were studied. At pH 7.0, the calculated quantities of undissociated acetic and butyric acids were insufficient to inhibit bacterial growth. The initial addition of acetate or butyrate at concentrations of 2.5 to 15 gL⁻¹ had distinct effects on the metabolism and growth of Clostridium butyricum. Acetate increased the biomass and butyrate production, reducing the lag time and 1,3-propanediol production. In contrast, the addition of butyrate induced an increase in 1,3-propanediol production (yield: 0.75 mol/mol glycerol, versus 0.68 mol/mol in the butyrate-free culture), and reduced the biomass and butyrate production. It was calculated that reduction of butyrate production could provide sufficient NADH to increase 1,3-propanediol production. The effects of acetate and butyrate highlight the metabolic flexibility of Cl. butyricum CNCM 1211 during glycerol fermentation. Received: 2 January 2001 / Accepted: 6 February 2001     

Aggregate-formation by Clostridium butyricum

Summary Clostridium butyricum was grown in a glucose-limited chemostat culture at a dilution rate of 0.1 h^–1 at pH 6.0. With 0.9% w/v input glucose in the medium the cells were found to grow in suspension and glucose was fermented completely to acetate and butyrate. An increase in the input concentration of glucose resulted in increased concentrations of end-products, but not all extra glucose was consumed. It could be demonstrated that this was due to a lowering of the maximal growth rate by elevated levels of butyric acid. However, prolonged growth in the presence of high glucose concentrations led to an increase in biomass. This was caused by the selection of a variant that was less sensitive to butyrate. This variant was able to form aggregates in an anaerobic gas-lift reactor at high dilution rates. Inoculation of these aggregates in a conventional chemostat culture with high glucose input resulted in an aggregated culture that remained stable for at least 6 months, and in which all glucose was consumed. Whether the organisms grew in suspension or in aggregates was found to be determined by the concentration of butyrate. The isolation of aggregate-forming variants from chemostat cultures leads to a very simple and new type of immobilization technique.Offprint requests to: G. R. Zoutberg     

Fermentation of raw glycerol to 1,3-propanediol by new strains ofClostridium butyricum

Industrial glycerol obtained through the transesterification process using rapeseed oil did not support growth of several strains ofClostridium butyricum obtained from bacterial culture collections. Ten new strains ofC. butyricum were obtained from mud samples from a river, a stagnant pond, and a dry canal. These new isolates fermented the commercial glycerol and produced 1,3-propanediol as a major fermentation product with concomitant production of acetic and butyric acids. Four of the ten isolates were able to grow on industrial glycerol obtained from rapeseed oil. One strain,C. butyricum E5, was very resistant to high levels of glycerol and 1,3-propanediol. Using fed-batch fermentation, 109 g L^–1 of industrial glycerol were converted into 58 g of 1,3-propanediol, 2.2 g of acetate and 6.1 g of butyrate per liter.     

Fermentation of mannitol by Clostridium butyricum: role of acetate as an external hydrogen acceptor

Summary The continuous fermentation of mannitol (pH 6, dilution rate (D)=0.087 h^-1) by Clostridium butyricum LMG 1213t1 was investigated under several conditions. Mannitol was readily fermented when glucose or acetate were added in the in-flow medium as co-substrate. Butyrate, CO₂ and H₂ were the major fermentation products. In mannitol-glucose mixtures (ratios 4 or 8) the amount of mannitol fermented depended upon the amount of glucose in the in-flow medium. In mannitol-acetate mixtures, 1 mol of acetate was needed for the fermentation of approximately 5.5 mol mannitol. We detected d-mannitol-1-phosphate dehydrogenase activity, responsible for the generation of supplementary reduced nicotine adenine dinucleotide (NADH) as a source for extra H₂ gas. Fermentation of mannitol-acetate in the presence of [¹⁴C]-labelled acetate revealed butyrate as the only labelled fermentation end-product.     

Energetics of growth of Microbacterium thermosphactum at low temperatures

Microbacterium thermosphactum was grown at 5°C and 9°C in glucose-limited continuous cultures. The end products of glucose metabolism were L-lactate and ethanol, and these compounds accounted for 86–92% of the glucose utilized. With input glucose concentrations less than 3 mM Y _glu ^Max was found to be 40–43, Y _ATP ^Max 20–21 and m _s 0.1–0.2. These values are almost identical to those found previously for cultures at 25°C and show that this psychrotroph grows with a very high energetic efficiency over a wide range of temperatures. With a higher (but still limiting) input glucose concentration of 5.6 mM at 9°C, cellular efficiency declined as there was a marked reduction in Y _glu. This decrease was accounted for in mathematical terms by an increase in m _s to 0.7, whilst Y _glu ^Max and Y _ATP ^Max remained high at 38 and 19 respectively.     

A mathematical model for the aerobic growth of Saccharomyces cerevisiae with a saturated respiratory capacity

A mathematical model for the aerobic growth of Saccharomyces cerevisiae in both batch and continuous culture is described. It was based on the experimental observation that the respiratory capacity of organism may become saturated and exhibit a maximum specific oxygen uptake rate after suitable adaptation. This experimental observation led to the possibility that transport into and out of the mitochondrion was of major importance in the overall metabolism of S. cerevisiae and was subject to long-term adaptation. Consistent with this observation a distributed model was proposed which. as its basis, assumed the control of repression or inhibition of the uptake rates of other substrates. No other regulation of fermentation and respiration was assumed. The model provided a suitable structure allowing precise quantification of the changes in rate and stoichiometry of energy production. The model clearly indicated that growth under the wide range of experimental conditions reported could not be predicted using constant values for the maximum specific respiratory rate of constant values of Y_ATP (g biomass/mol ATP) and PO ratio of (mol ATP/atom oxygen). The causes of the variation in the respiratory rate were not determined and it was concluded that a more detailed analysis (reported subsequently) was required. The variation of Y_ATP and PO ratio with specific growth rate implied that the efficiency of ATP generation or ATP utilization decreased with increasing specific growth rate. It was concluded that it was not possible to quantify the individual effect of Y_ATP and PO ratio until independent means for their reliable estimation is available.     

Control of the selectivity of butyric acid production and improvement of fermentation performance withClostridium tyrobutyricum

Summary The parameters that control fermentation performance of butyrate production have been studied with a selected strain ofClostridium tyrobutyricum. Fed-batch supply of glucose increased productivity for butyrate. The ratio of butyrate to total acids was strongly influenced by the growth rate of the bacteria, acetate being produced along with butyrate at higher growth rates. In glucose-limited, fed-batch cultures, initially produced acetate was re-utilized, resulting in exclusive production of butyrate. In cultures with non-limiting glucose feeding, the butyrate concentration reached 42.5 g·1^–1 with a selectivity of 0.90, a productivity of 0.82 g·^–1 per hour and a yield of 0.36 g·g^–1 The effects of the mode of supply of glucose on the production of butyrate and acetate are discussed in relation with the energy requirements for cell growth.     

Influence of metabolic end-products on the growth efficiency ofKlebsiella aerogenes in anaerobic chemostat culture

Progressively increasing the input concentration of growth-limiting nutrient (glucose, ammonia, K⁺) to anaerobic chemostat cultures ofKlebsiella aerogenes (D=0.38 h⁻¹; 35°C; pH 6.8) led to a non-linear increase in bacterial cell concentration. At modest population densities, residual growth-limiting substrate levels increased substantially, with increasing input concentration, and the culture bacterial dry weight tended to a constant value. With the glucose-limited culture, increasing the glucose input concentration above 20 g·1⁻¹ led to accumulation of unused glucose and a change in the fermentation pattern. There was a concomitant lowering of the yield value with respect to glucose consumption, and the calculated Y_ATP value similarly declined. Addition of extra essential (non-limiting) nutrients to the culture was without effect. Similarly, addition of individual fermentation products (acetate, ethanol,d-lactate, 2,3-butanediol, succinate) to the feed medium, in varying concentrations and in different combinations, failed to influence the fermentation pattern or the energetics of cell synthesis. However, a clear correlation was observed between the yield values (of both glucose- and K⁺-limited cultures) and the steady state concentration of CO₂ in the effluent gas. Increasing the concentration CO₂ either by increasing the population density or lowering the sparging rate of nitrogen gas through the culture, effected a lowering of the yield values. It is suggested that dissolved CO₂ exerts an effect on both metabolism and the energetics of cell synthesis. A possible mechanism of energy dissipation (i.e., a futile cycle) involving carboxylation and decarboxylation reactions is proposed.     

Growth characteristics of Saccharomyces cerevisiae S288C in changing environmental conditions: auxo-accelerostat study

The effect of individual environmental conditions (pH, pO₂, temperature, salinity, concentration of ethanol, propanol, tryptone and yeast extract) on the specific growth rate as well as ethanol and glycerol production rate of Saccharomyces cerevisiae S288C was mapped during the fermentative growth in aerobic auxo-accelerostat cultures. The obtained steady-state values of the glycerol to ethanol formation ratio (0.1 mol mol⁻¹) corresponding to those predicted from the stoichiometric model of fermentative yeast growth showed that the complete repression of respiration was obtained in auxostat culture and that the model is suitable for calculation of Y _ATP and Q _ATP values for the aerobic fermentative growth. Smooth decrease in the culture pH and dissolved oxygen concentration (pO₂) down to the critical values of 2.3 and 0.8%, respectively, resulted in decrease in growth yield (Y _ATP) and specific growth rate, however the specific ATP production rate (Q _ATP) stayed almost constant. Increase in the concentration of biomass (>0.8 g dwt l⁻¹), propanol (>2 g l⁻¹) or NaCl (>15 g l⁻¹) lead at first to the decrease in the specific growth rate and Q _ATP, while Y _ATP was affected only at higher concentrations. The observed decrease in Q _ATP was caused by indirect rather than direct inhibition of glycolysis. The increase in tryptone concentration resulted in an increase in the specific growth rate from 0.44 to 0.62 h⁻¹ and Y _ATP from 12.5 to 18.5 mol ATP g dwt⁻¹. This study demonstrates that the auxo-accelerostat method, besides being an efficient tool for obtaining the culture characteristics, provides also decent conditions for the experiments elucidating the control mechanisms of cell growth.     

A re-assessment of bacterial growth efficiency: the heat production and membrane potential of Streptococcus bovis in batch and continuous culture

Glucose-limited, continuous cultures (dilution rate 0.1 h^-1) of Streptococcus bovis JB1 fermented glucose at a rate of 3.9 mol mg protein^-1 h^-1 and produced acctate, formate and ethanol. Based on a maximum ATP yield of 32 cells/mol ATP (Stouthamer 1973) and 3 ATP/glucose, the theoretical glucose consumption for growth would have been 2.1 mol mg protein^-1 h^-1. Because the maintenance energy requirement was 1.7 mol/mg protein/h (Russell and Baldwin 1979), virtually all of the glucose consumption could be explained by growth and maintenance and the Y_ATP was 30. Glucose-limited, continuous cultures produced heat at a rate of 0.29 mW/mg protein, and this value was similar to the enthalpy change of the fermentation (0.32 mW/mg protein). Batch cultures (specific growth rate 2.0 h^-1) fermented glucose at a rate of 81 mol mg protein^-1 h^-1, and produced only lactate. The heat production was in close agreement with the theoretical enthalpy change (1.72 versus 1.70 mW/mg protein), but only 80% of the glucose consumption could be accounted by growth and maintenance. The Y_ATP of the batch cultures was 25. Nitrogen-limited, glucose-excess, non-growing cultures fermented glucose at a rate of 6.9 mol mg protein^-1 h^-1, and virtually all of the enthalpy for this homolactic fermentation could be accounted as heat (0.17 mW/mg protein). The nitrogenlimited cultures had a membrane potential of 150 mV, and nearly all of the heat production could be explained by a futile cycle of protons through the cell membrane (watts = amperes x voltage where H⁺/ATP was 3). The membrane voltage of the nitrogen-limited cells was higher than the glucose-limited continuous cultures (150 versus 80 mV), and this difference in voltage explained why nitrogen-limited cultures consumed glucose faster than the maintenance rate. Batch cultures had a membrane potential of 100 mV, and this voltage could not account for increased glucose consumption (more than growth plus maintenance). It appears that another mechanism causes the increased heat production and lower growth efficiency of batch cultures.     

Thermobacteroides acetoethylicus gen. nov. and spec. nov., a new chemoorganotrophic,anaerobic, thermophilic bacterium

The taxonomic and metabolic characteristics of a new caldoactive bacterium, Thermobacteroides acetoethylicus, that is prevalent in volcanic features where organic matter is vigorously being decomposed is described. T. acetoethylicus is a nonsporing, obligately anaerobic rod that stains gram-negative and exists singly or in pairs. Electron micrographs revealed peritrichous flagellation and a distinctive outer wall envelope structure without an outer wall membrane layer. The temperature range for growth was >40°C and <80°C; the pH range was between 5.5 and 8.5. The DNA base composition was 31±1 mol% guanosine plus cytosine. Fermentable carbohydrates included glucose, mannose, cellobiose, lactose, maltose, sucrose and starch. Growth on glucose in complex medium was associated with a 30 min doubling time; and ethanol, acetate, H₂/CO₂, butyrate and isobutyrate accounted for a balanced fermentation. Lactic acid was not formed. Growth was inhibited by O₂, 2% NaCl, penicillin, streptomycin, vankomycin and neomycin, but not by chloramphenicol or hydrogen (2 atm). Glucose was metabolized via the Embden-Meyerhoff Pathway. A molar growth yield of 18.3 g cell per mol glucose and an ATP yield of 8 g cell per mol ATP produced was obtained. These results support the absence of detectable cytochromes and suggest that energy conservation is via substrate level phosphorylation alone.Abbreviations DNA deoxyribonucleic acid - ATP adenosine triphosphate - LPBB low phosphate buffered basal - TYEG tryptone yeast extract glucose - O.D. optical density - Y _ATP molar ATP yield - G+C guanosine plus cytosine