Quantitative comparison of lactose and glucose utilization in Bifidobacterium longum cultures

In batch cultures, Bifidobacterium longum SH2 has a higher final cell concentration and greater substrate consumption when grown on lactose versus glucose. Continuous cultures were used to compare lactose and glucose utilization by B. longum quantitatively. In the continuous culture, the estimated maintenance coefficients (m) were similar when on lactose and glucose; the maximum cell yield coefficient (Y(X/S)(max)) was higher on lactose; and the specific consumption rate of lactose (q(S)) was lower than that of glucose. Assuming that cell growth followed the Monod model, the maximum specific growth rates (mu(max)) and saturation constants (K(S)) in lactose and glucose media were determined using the Hanes-Woolf plots. The respective values were 0.40 h(-)(1) and 78 mg/L for lactose and 0.46 h(-)(1) and 697 mg/L for glucose. The kinetic parameters of the continuous cultures showed that B. longum preferred lactose to glucose, although the specific consumption rate of glucose was higher than that of lactose.     

Morphology and physiology of an alpha-amylase producing strain of Aspergillus oryzae during batch cultivations

The microscopic morphology, that is, total hyphal length and total number of tips, has been characterized during batch cultivations of Aspergillus oryzae. The specific growth rate estimated by measuring the total hyphal length (mu(h)) corresponds well with the specific growth rate estimated from dry weight measurements during cultures grown as free hyphal elements. The average tip extension rate can be described with a saturation type kinetics with respect to the average total hyphal length, and the branching frequency is closely related to the total hyphal length. For the applied strain of A. oryzae, pellet formation occurs by coagulation of spores. The agglomeration process is pH dependent and pellets are formed at pH values higher than 5, whereas low pH (<3.5) results in growth as freely dispersed hyphal elements. The maximum specific growth rate has a broad pH optimum between 3 and 7, whereas the alpha-amylase production has a sharper maximum at about pH 6. During batch cultivation with pellets the growth is described well by the cube-root law when pellet fragmentation can be neglected. The kinetic parameter k in the cube-root law is derived from the growth kinetics with no mass transfer limitation, k = mu(h)/3. Based on an oxygen balance, the active growth layer in the pellet is estimated to be 200 to 325 mum and, consequently, up to 50% of the biomass is limited by oxygen for large pellets. Ethanol production (up to 1 g L(-1)) was observed during batch cultivations with pellets, suggesting that ethanol is produced in the oxygen limited part of the biomass. A constitutive, low alpha-amylase production was observed at high glucose concentration. The specific alpha-amylase production was significantly higher for filamentous growth than for pellets and oxygen appears to be necessary for production of alpha-amylase. (c) 1996 John Wiley & Sons, Inc.     

Modeling Pichia pastoris growth on methanol and optimizing the production of a recombinant protein, the heavy-chain fragment C of botulinum neurotoxin, serotype A

An unstructured growth model for the recombinant methylotrophic yeast P. pastoris Mut(+) expressing the heavy-chain fragment C of botulinum neurotoxin serotype A [BoNT/A(H(c))], was successfully established in quasi-steady state fed-batch fermentations with varying cell densities. The model describes the relationships between specific growth rate and methanol concentration, and the relationships between specific methanol and ammonium consumption rates and specific growth rate under methanol-limited growth conditions. The maximum specific growth rate (mu) determined from the model was 0.08 h(-1) at a methanol concentration of 3.65 g/L, while the actual maximum mu was 0.0709 h(-1). The maximum specific methanol consumption rate was 0.0682 g/g WCW/h. From the model, growth can be defined as either methanol-limited or methanol-inhibited and is delineated at a methanol concentration of 3.65 g/L. Under inhibited conditions, the observed biomass yield (Y(X/MeOH)) was lower and the maintenance coefficient (m(MeOH)) was higher than compared to limited methanol conditions. The Y(X/MeOH) decreased and m(MeOH) increased with increasing methanol concentration under methanol-inhibited conditions. BoNT/A(H(c)) content in cells (alpha) under inhibited growth was lower than that under limited growth, and decreased with increasing methanol concentration. A maximum alpha of 1.72 mg/g WCW was achieved at a mu of 0.0267 h(-1) and induction time of 12 h.     

Physiological characterization and fed-batch production of an extracellular maltase of Schizosaccharomyces pombe CBS 356

The fission yeast Schizosaccharomyces pombe CBS 356 exhibits extracellular maltase activity. This activity may be of commercial interest as it exhibited a low pH optimum (3.5) and a high affinity for maltose (Km of 7.0+/-1.8 mM). N-terminal sequencing of the protein indicates that it is the product of the AGL1 gene. Regulation of this gene occurs via a derepression/repression mechanism. In sugar- or nitrogen-limited chemostat cultures, the specific rate of enzyme production (q(p)) was independent of the nature of the carbon source (i.e. glucose or maltose), but synthesis was partially repressed by high sugar concentrations. Furthermore, q(p) increased linearly with specific growth rate (mu) between 0.04 and 0.10 h(-1). The enzyme is easily mass-produced in aerobic glucose-limited fed-batch cultures, in which the specific growth rate is controlled to prevent alcoholic fermentation. In fed-batch cultures in which biomass concentrations of 83 g L(-1) were attained, the enzyme concentration reached 58,000 Units per liter culture supernatant. Extracellular maltase may be used as a dough additive in order to prevent mechanisms such as maltose-induced glucose efflux and maltose-hypersensitivity that occur in maltose-consuming Saccharomyces cerevisiae.     

Fermentative capacity in high-cell-density fed-batch cultures of baker's yeast

High-cell-density fed-batch processes for bakers' yeast production will involve a low-average-specific growth rate due to the limited oxygen-transfer capacity of industrial bioreactors. The relationship between specific growth rate and fermentative capacity was investigated in aerobic, sucrose-limited fed-batch cultures of an industrial bakers' yeast strain. Using a defined mineral medium, biomass concentrations of 130 g dry weight/L were reproducibly attained. After an initial exponential-feed phase (mu = 0.18 h(-1)), oxygen-transfer limitation necessitated a gradual decrease of the specific growth rate to ca. 0.01 h(-1). Throughout fed-batch cultivation, sugar metabolism was fully respiratory, with a biomass yield of 0.5 g biomass/g sucrose(-1). Fermentative capacity (assayed off-line as ethanol production rate under anaerobic conditions with excess glucose) showed a strong positive correlation with specific growth rate. The fermentative capacity observed at the end of the process (mu = 0.01 h(-1)) was only half that observed during the exponential-feed phase (mu = 0.18 h(-1)). During fed-batch cultivation, activities of glycolytic enzymes, pyruvate decarboxylase and alcohol dehydrogenase in cell extracts did not exhibit marked changes. This suggests that changes of fermentative capacity during fed-batch cultivation were not primarily caused by regulation of the synthesis of glycolytic enzymes.     

Effects of Chinese wolfberry (Lycium chinense P. Mill.) leaf hydrolysates on the growth of Pediococcus acidilactici

Growth stimulating effects of LYCH leaf hydrolysates on Pediococcus acidilactici IMT101 cells were observed when MRS broth was supplemented with 20% (v/v) H1+H2, the mixture of hydrolysates prepared by a traditional tea-making process. Cells grown on MRS containing H1+H2 showed a shortened lag phase while yielding a cell concentration (X(s)) significantly higher than other conditions investigated entering stationary phase. The maximal specific growth rate (mu(max)) was also the highest among all. Microwave-assisted extraction (MAE) at 80 degrees C for 2h (M80(2h)) released more amino acids but less sugar (fructose, glucose, and sucrose) than in H1+H2. Both X(s) and mu(max) reached in M80(2h)-supplemented MRS broth were lower than those in MRS containing H1+H2. No correlations between amino acids and cell growth were found. P. acidilactici cells grown in MRS broth in general showed higher consumption of carbohydrate in comparison with those in M17 broth containing the same carbohydrate. In the absence of FOS, the increased glucose concentration in MRS when supplemented by H1+H2 hydrolysates appeared to be responsible for the stimulatory effects on P. acidilactici growth. The growth-enhancing effects of LYCH leaf hydrolysates indicate the potential of developing new applications for LYCH leaves in promoting the growth of other probiotic cells using a simple process.     

Morphology of Mycoplasma laidlawii type A. II. Effect of glucose on growth and cellular morphology

Anderson, D. L. (University of Minnesota, Minneapolis), M. E. Pollock, and L. F. Brower. Morphology of Mycoplasma laidlawii type A. II. Effect of glucose on growth and cellular morphology. J. Bacteriol. 90:1768-1777. 1965.-Cells of Mycoplasma laidlawii A grown in soy peptone-yeast extract (SP-YE) broth reached higher maximal titers than cells grown in SP-YE supplemented with 0.2% glucose, and remained viable longer than glucose-grown cells. Moreover, addition of glucose to SP-YE markedly affected the morphological developmental sequence of the organism. The diameter of glucose-grown cells at 28 to 40 hr was often two to four times that of cells grown without glucose; these large glucose-grown cells deteriorated progressively, and presumably liberated 0.1- to 0.25-mu small bodies. In contrast, pleomorphic 22- to 28-hr cells grown in SP-YE without glucose gave rise to uniform bodies 0.5 to 1.0 mu in diameter; limited numbers of 0.1- to 0.25-mu small bodies were also liberated in nonglucose cultures after 45 to 64 hr. Electron-microscopic counts of 16- to 64-hr cultures agreed well with counts of colony-forming units (CFU) when organisms larger than 0.25 mu were included in the microscopic counts. Small bodies, 0.1 to 0.25 mu in diameter, apparently did not contribute substantially to numbers of CFU. Droplet patterns of cells grown in Arginine Assay Medium and L15 Tissue Culture Medium were cleaner than patterns of cells grown in SP-YE.     

Growth-rate-independent production of recombinant glucoamylase by Fusarium venenatum JeRS 325

Most recombinant proteins generated in filamentous fungi are produced in fed-batch cultures, in which specific growth rate normally decreases progressively with time. Because of this, such cultures are more suited to the production of products that are produced efficiently at low-growth rates (e.g., penicillin) than to products which are produced more efficiently at high-growth rates (e. g., glucoamylase). Fusarium venenatum A3/5 has been transformed (JeRS 325) to produce Aspergillus niger glucoamylase (GAM) under the control of the Fusarium oxysporum trypsin-like protease promoter. No glucoamylase was detected in the culture supernatant during exponential growth of F. venenatum JeRS 325 in batch culture. In glucose-limited chemostat cultures, GAM concentration increased with decrease in dilution rate, but the specific production rate of GAM (g GAM [g biomass](-1) h(-1)) remained approximately constant over the dilution-rate range 0.05 h to 0.19 h(-1), i.e., the recombinant protein was produced in a growth-rate-independent manner. The specific production rate decreased at dilution rates of 0.04 h(-1) and below. Specific production rates of 5.8 mg and 4.0 mg GAM [g biomass](-1) h(-1) were observed in glucose-limited chemostat cultures in the presence and absence of 1 g mycological peptone L(-1). Compared to production in batch culture, and for the same final volume of medium, there was no increase in glucoamylase production when cultures were grown in fed-batch culture. The results suggested that a chemostat operated at a slow dilution rate would be the most productive culture system for enzyme production under this trypsin-like promoter.     

The effect of the dilution rate on CHO cell physiology and recombinant interferon-gamma production in glucose-limited chemostat culture

The physiology of a recombinant Chinese hamster ovary cell line in glucose-limited chemostat culture was studied over a range of dilution rates (D = 0.008 to 0.20 h(-1)). The specific growth rate (mu) deviated from D at low dilution rates due to an increased specific death rate. Extrapolation of these data suggested a minimum specific growth rate of 0.011 h(-1) (mu(max) = 0.025 h(-1)) The metabolism at each steady state was characterized by determining the metabolic quotients for glucose, lactate, ammonia, amino acids, and interferon-gamma (IFN-gamma). The specific rate of glucose uptake increased linearly with mu, and the saturation constant for glucose (K(s)) was calculated to be 59.6 muM. There was a linear increase in the rate of lactate production with a higher yield of lactate from glucose at high growth rates. The decline in the rate of production of lactate, alanine, and serine at low growth rate was consistent with the limitation of the glycolytic pathway by glucose. The specific rate of IFN-gamma production increased with mu in a manner indicative of a growth-related product. Despite changes in the IFN-gamma production rate and cell physiology, the pattern of IFN-gamma glycosylation was similar at all except the lowest growth rates where there was increased production of nonglycosylated IFN-gamma. (c) 1993 John Wiley & Sons, Inc.     

Comparative physiology of two protozoan parasites, Leishmania donovani and Trypanosoma brucei, grown in chemostats.

Cultures of the insect stage of the protozoan parasites Leishmania donovani and Trypanosoma brucei were grown in chemostats with glucose as the growth rate-limiting substrate. L. donovani has a maximum specific growth rate (mu max) of 1.96 day-1 and a Ks for glucose of 0.1 mM; the mu max of T. brucei is 1.06 day-1 and the Ks is 0.06 mM. At each steady state (specific growth rate, mu, equals D, the dilution rate), the following parameters were measured: external glucose concentration (Glcout), cell density, dry weight, protein, internal glucose concentration (Glcin), cellular ATP level, and hexokinase activity. L. donovani shows a relationship between mu and yield that allows an estimation of the maintenance requirement (ms) and the yield per mole of ATP (YATP). Both the ms and the YATP are on the higher margin of the range found for prokaryotes grown on glucose in a complex medium. L. donovani maintains the Glcin at a constant level of about 50 mM as long as it is not energy depleted. T. brucei has a decreasing yield with increasing mu, suggesting that it oxidizes its substrate to a lesser extent at higher growth rates. Glucose is not concentrated internally but is taken up by facilitated diffusion, while phosphorylation by hexokinase is probably the rate-limiting step for glucose metabolism. The Ks is constant as long as glucose is the rate-limiting substrate. The results of this study demonstrate that L. donovani and T. brucei have widely different metabolic strategies for dealing with varying external conditions, which reflect the conditions they are likely to encounter in their respective insect hosts.     

Kinetic Analyses of Desulfurization of Dibenzothiophene by Rhodococcus erythropolis in Continuous Cultures

Rhodococcus erythropolis N1-36, a desulfurization strain, was grown in continuous culture at 10 different dilution rates with 50 (mu)M dibenzothiophene sulfone (DBTO(inf2)) as the growth-limiting nutrient. The steady-state biomass, concentrations of substrate (DBTO(inf2)) and product (monohydroxybiphenyl), saturation constant (0.39 (mu)M DBTO(inf2)), and cell yield coefficient (9 mg of biomass(middot)(mu)M(sup-1) DBTO(inf2)) were measured. Continuous cultures at five temperatures allowed calculation of activation energy (0.84 kcal(middot)mol(sup-1) [ca. 3.5 kJ(middot)mol(sup-1)]) near the optimal temperature (30(deg)C) for growth. A washout technique was used to calculate the maximum specific growth rate (0.235 h(sup-1)), a value equivalent to a minimum generation time of 2.95 h.     

Sand administration as an instrument for biofilm control of Pseudomonas putida ATCC 11172 in chemostat cultures

Pseudomonas putida ATCC 11172 was grown in chemostat on L-asparagine or phenol as the sole, limiting carbon and energy source. The growth characteristics of a culture where a biofilm was present, were compared with one where the biofilm was strongly reduced by the grinding and shearing effect of sand suspended in the culture. In the presence of the intact biofilm, the curve of steady-state biomass versus dilution rate diverged greatly from the theoretical pattern predicted by conventional chemostat models. The sand strongly retarded the biofilm formation and to a high degree restored the shape of the biomass versus dilution rate curve to a more conventional pattern. The maximum specific growth rate (mu(max)) could not be calculated from the biofilm cultures. However using the sand cultures, mu(max) was determined to 0.64 h(-1) with L-asparagine as the carbon source and 0.49 h(-1) with phenol which compare favorably with the respective mu(max) values calculated from batch cultures.Incorporation of sand into strongly agitated cultures is recommended as an efficient and simple means of controlling biofilm formation in continuous cultures. The method may enable the gathering of basic kinetic data difficult to obtain in the presence of biofilm.     

Biodegradation of octylphenol polyethoxylate surfactant Triton X-100 by selected microorganisms

Octylphenol polyethoxylate (OPEO(n)) surfactants are used in numerous commercial and industrial products. Large amounts of such surfactants and their various residual biodegradation by-products are ultimately released into the environment. OPEO(n) biodegradation was performed in this study using pure cultures of Pseudomonas species and strains under different environmental conditions. Environmental factors including the pH, nitrogen sources, and growth kinetics of the cells were investigated. The intermediates of Triton X-100 biotransformation were detected by high performance liquid chromatography-mass spectrophotograph (HPLC-MS). We found the highest specific growth rate (mu) was 0.56 h(-1) and this was achieved by strain E with an initial concentration of Triton X-100 of 5000 mg L(-1). A pH level of 7 was most favorable for cell growth for all five strains. The highest specific growth rate was achieved using (NH(4))(2)SO(4) as the sole nitrogen source for strain E. Strain A showed an enhancement of growth when between 0.2 and 1.4 mg L(-1) of H(2)O(2) was added. Detection of intermediates was possible after four days of transformation and the octylphenol triethoxylate (OPEO(3)) peak was predominant, while the high molecular weight peaks had all disappeared. The kinetic analysis demonstrated that the greatest maximum specific growth rate (mu(max)) and the greatest saturation constant (K(s)) of 0.83 h(-1) and 5.24 mg L(-1), respectively, were obtained for strain E in 5000 mg L(-1) Triton X-100. The higher K(i) revealed that strain A was resistant to higher Triton X-100 concentrations.     

Catabolic control of hybridoma cells by glucose and glutamine limited fed batch cultures

Substrate limited fed batch cultures were used to study growth and overflow metabolism in hybridoma cells. A glucose limited fed batch, a glutamine limited fed batch, and a combined glucose and glutamine limited red batch culture were compared with batch cultures. In all cultures mu reaches its maximum early during growth and decreases thereafter so that no exponential growth and decreases thereafter so that no exponential growth rate limiting, although the glutamine concentration (>0.085mM) was lower than reported K(s) vales and glucose was below 0.9mM; but some other nutrients (s) was the cause as verified by simulations. Slightly more cells and antibodies were produced in the combined fed batch compared with the batch culture. The specific rates for consumption of glucose and glutamine were dramatically influenced in fed batch cultures resulting in major metabolic changes. Glucose limitation decreased lactate formation, but increased glutamine consumption and ammonium formation. Glutamine limitation decreased ammonium and alanine formation of lactate, alanine, and ammonium was negligible in the dual-substrate limited fed batch culture. The efficiency of the energy metabolism increased, as judged by the increase in the cellular yield coefficient for glucose by 100% and for glutamine by 150% and by the change in the metabolic ratios lac/glc, ala/ln, and NH(x)/ln, in the combined fed culture. The data indicate that a larger proportion of consumed glutamine enters the TCA cycle through the glutamate dehydrogenase pathway, which releases more energy from glutamine than the transamination pathway. We suggest that the main reasons for these changes are decreased uptake rates of glucose and glutamine, which in turn lead to a reduction of the pyruvate pool and a restriction of the flux through glutaminase and lactate dehydrogenase. There appears to be potential for further cell growth in the dual-substrate-limited fed batch culture as judged by a comparison of mu in the different cultures. (c) 1994 John Wiley & Sons, Inc.     

Production of tissue plasminogen activator (t-PA) in Aspergillus niger

A protease-deficient strain of Aspergillus niger has been used as a host for the production of human tissue plasminogen activator (t-PA). In defined medium, up to 0.07 mg t-PA (g biomass)(-1) was produced in batch and fed-batch cultures and production was increased two- to threefold in two-phase batch cultures in which additional glucose was provided as a single pulse at the end of the first batch growth phase. Production was increased [up to 1.9 mg t-PA (g biomass)(-1)] by the addition of soy peptone to the defined medium. The rate of t-PA production in batch cultures supplemented with soy peptone (0.2 to 0.6 mg t-PA L(-1) h(-1)) was comparable to rates observed previously in high-producing mammalian or insect cell cultures. In glucose-limited chemostat culture supplemented with soy peptone, t-PA was produced at a rate of 0.7 mg t-PA L(-1) h(-1). Expression of t-PA in A. niger resulted in increased expression of genes (bipA, pdiA, and cypB) involved in the unfolded protein response (UPR). However, when cypB was overexpressed in a t-PA-producing strain, t-PA production was not increased. The t-PA produced in A. niger was cleaved into two chains of similar molecular weight to two-chain human melanoma t-PA. The two chains appeared to be stable for at least 16 h in culture supernatant of the host strain. However, in general, <1% of the t-PA produced in A. niger was active, and active t-PA disappeared from the culture supernatant during the stationary phase of batch cultures, suggesting that the two-chain t-PA may have been incorrectly processed or that initial proteolytic cleavage occurred within the proteolytic domain of the protein. Total t-PA (detected by enzyme-linked immunoassay) also eventually disappeared from culture supernatants, confirming significant extracellular proteolytic activity, even though the host strain was protease-deficient.     

Kinetic parameters and thermodynamic values of beta-xylosidase production by Kluyveromyces marxianus

Kinetic parameters for production of beta-xylosidase by Kluyveromyces marxianus were determined in growth media containing glucose, xylose, cellobiose, sucrose and lactose as carbon sources. K. marxianus achieved maximum beta-xylosidase specific product yield (Y(P/X)) when grown on xylose. Basal level of activity was achieved in cultures grown on glucose. Kinetic parameters of enzyme production and cell mass formation were correlated. Enzyme synthesis was regulated by an induction mechanism and growth-dependent repression mechanism. Thermodynamic analysis revealed that the cell system exerted protection against thermal inactivation. A partially purified enzyme showed good stability when incubated at 60 degrees C and was quite stable at a pH of 5.0-7.0 and may be exploited for commercial applications.     

Characterization of nerolidol biotransformation based on indirect on-line estimation of biomass concentration and physiological state in batch cultures of Aspergillus niger

Biotransformation of the sesquiterpenoid trans-nerolidol by Aspergillus niger has previously been investigated as a method for the formation of 12-hydroxy-trans-nerolidol, a precursor in the synthesis of the industrially interesting flavor alpha-sinensal. We characterized biotransformations of cis-nerolidol, trans-nerolidol, and a commercially available cis/trans-nerolidol mixture in repeated batch cultures of A. niger grown in computer-controlled bioreactors. On-line quantification of titrant addition in pH control allowed characterization of (1) maximal specific growth rate in exponential growth phases, (2) exponential induction of acid formation in postexponential phases, (3) inhibition of organic acid formation after nerolidol addition, and (4) exponential recovery from this inhibition. Addition of a (+/-)-cis/trans-nerolidol mixture during exponential or postexponential phase to cultures grown in minimal medium at high dissolved oxygen tension (above 50% air saturation), to cultures at low dissolved oxygen tension (5% air saturation), or to cultures grown in rich medium demonstrated that the physiological state before nerolidol addition had a major influence on biotransformation. The maximal molar yield of 12-hydroxy-trans-nerolidol (9%) was obtained by addition of a (+/-)-cis/trans-nerolidol mixture to the culture in the postexponential phase at high dissolved oxygen tension in minimal medium. Similar yields were obtained in rich medium, where the rate of biotransformation was doubled.     

The pH mediated effects of initial glucose concentration on the transitory occurrence of extracellular metabolites, gas exchange and growth yields of aerobic batch cultures of Klebsiella pneumoniae

The changes in growth kinetics in aerobic batch cultures of Klebsiella pneumoniae were followed by measurements of extracellular metabolites, rates of gas exchange, dissolved oxygen tension, pH, and carbon balance at all stages of growth. When the initial growth-limiting glucose concentration in media without pH control was increased from 1.0 g carbon L(-1) to 2.2 g carbon L(-1), the number of different, mainly acidic, extracellular metabolites of glucose at the end of exponential growth increased, while the proportion of acetate decreased. During the postexponential growth phase, the extracellular metabolites were oxidized, resulting in an increasing complexity of changes in pH, gas exchange, and dissolved oxygen tension with increasing initial substrate concentration. All these parameters showed concomitant stepwise changes. This pattern was independent of the dissolved oxygen tension in the range 30-200 muM. When pH was kept constant, the number, slope, and relative magnitude of the steps in gas exchange and dissolved oxygen tension were pH-dependent, being most complex at low pH. Detailed carbon balances showed that 20% of the initial glucose was converted into extracellular metabolites at the end of exponential growth at neutral pH. In the postexponential phase, pyruvate (2%) was reoxidized first followed by acetate (13%). The observed molar growth yield coefficient (Y(ATP)) was 8.4 if the transitory occurrence of pyruvate and acetate was accounted for, and 6.4 if it was neglected. The corrected observed molar growth yield coefficient (Y'(ATP)) was 9.4 and compared well with the true molar growth yield coefficient (Y(Max) (ATP)), which was found to be 11.0. Specific in situ respiration rates of the exponential growth phase of cultures grown at different controlled pH values compared well with in situ values for energy-limited chemostat grown cells at the same growth rates, suggesting that growth in the batch culture was energy-limited throughout the exponential growth phase. This view was supported by low levels of intracellular glycogen and exopolysaccharides of all cultures, by the value of Y'(ATP) of 9.4, and by a constant specific production rate of the extracellular metabolites throughout exponential growth. It was concluded that even under strictly aerobic conditions, control of pH is as important as control of dissolved oxygen tension during growth of enterobacteriaceae in batch cultures.     

Kinetics and morphology of glucose-limited cultures of moulds grown in a chemostat and on solid media.

The affinity (KS value) of Geotrichum candidum for glucose determined from chemostate cultures was ca. 1 mg/1. KS values for glucose was also estimated from the radial growth rates of colonies of G. candidum and Neurospora crassa grown on media solidified with agar or silica gel. An assessment is made of the use of colony radial growth rate to determine substrate affinities. The length of apical and intercalary hyphal comparte ments, internode length and the diameter of leading hyphaat the margin of colonies grown on solid media were all reduced at low glucose concentrations.     

Cultural properties and mass-energy balances in methanol fermentation by Methylomonas methanolovorans

The cultural properties of an obligate methanol utilizer, Methylomonas methanolovorans, were investigated in batch and continuous cultures, and the problems of mass-energy balances were examined. Among the culture data, an exponential increase of growth lag with increased methanol concentration, as well as the inhibition kinetics in the relation between attainable maximum specific growth rate (mu(m) <== 0.52) and methanol concentration are of interest. In the latter case, the inhibition constant (K(i)) and the index number were 40 g/L, and 3 (dimensionless), respectively. The maximum yield coefficient (Y) in both batch and chemostat cultures was around 0.52. An analysis of the behavior of respiratory activity (Q(o2)) in response to the dissolved oxygen concentration (DO) indicated that the oxygen-terminal entity should be regarded as a single one with a saturation constant for DO of 32 mug/L (1.1 x 10(-6)M). Chemostat data showed that the saturation constant for methanol is as low as 2.2 mg/L or 7 x 10(minus;5)M. A linear relationship was observed between the respiratory activity (mol O(2)g(-1)h(-1)) and the specific growth rate (mu i h(-1)), with the relationship Q(o2) = 0.0504mu + 0.00112. The theory of mass and energy balances used by Roels has been reformed to give useful relationships between RQ or the cell yield and mu. In the case of M. methanolovorans, the relations can be greatly simplified since the influence of metabolic by-product formation was negligible. Experimental RQ values (theoretical values for Y = 0.52 and 0.445) at varying mu-values were compared with theoretical ones; despite considerable fluctuations, the results were regarded to conform with theory. By use of mass balance equations and enthalpy data of known compounds, the heat evolution in methanol fermentation was estimated indirectly to be 612 kcal/100 g biomass formed. The Y(ATP) problems are also discussed.