Regulation of photosynthetic electron-transport in Phaseolus vulgaris L., as determined by room-temperature chlorophyll a fluorescence

The regulation of photosystem II (PSII) by light-, CO₂-, and O₂-dependent changes in the capacity for carbon metabolism was studied. Estimates of the rate of electron transport through PSII were made from gas-exchange data and from measurements of chlorophyll fluorescence. At subsaturating photon-flux density (PFD), the rate of electron transport was independent of O₂ and CO₂. Feedback on electron transport was observed under two conditions. At saturating PFD and low partial pressure of CO₂, p(CO₂), the rate of electron transport increased with p(CO₂). However, at high p(CO₂), switching from normal to low p(O₂) did not affect the net rate of photosynthetic CO₂ assimilation but the rate of electron-transport decreased by an amount related to the change in the rate of photorespiration. We interpret these effects as 1) regulation of ribulose-1,5-bisphosphatecarboxylase (RuBPCase, EC 4.1.1.39) activity to match the rate of electron transport at limiting PFD, 2) regulation of electron-transport rate to match the rate of RuBPCase at low p(CO₂), and 3) regulation of the electron-transport rate to match the capacity for starch and sucrose synthesis at high p(CO₂) and PFD. These studies provide evidence that PSII is regulated so that the capacity for electron transport is matched to the capacity for other processes required by photosynthesis, such as ribulose-bisphosphate carboxylation and starch and sucrose synthesis. We show that at least two mechanisms contribute to the regulation of PSII activity and that the relative engagement of these mechanisms varies with time following a step change in the capacity for ribulose-bisphosphate carboxylation and starch and sucrose synthesis. Finally, we take advantage of the relatively slow activation of deactivated RuBPCase in vivo to show that the activation level of this enzyme can limit the rate of electron transport as evidenced by increased feedback on PSII following a step change in p(CO₂). As RuBPCase as activated, the feedback on PSII declined.Abbreviations and symbols J_C electron-transport rate calculated from CO₂-assimilation measurements - J_F electron-transport rate calculated from fluorescence parameters - PFD photon-flux density - q_E energy-dependent quenching - PSII photosystem II - q_Q Q-dependent quenching - QY quantum yield - RuBPCase ribulose-1,5-bisphosphate carboxylase (EC 4.1.1.39) C.I.W. publication No. 1015     

Electron-transport chain and coupled oxidative phosphorylation in methanol-grown Paracoccus denitrificans

Methanol dehydrogenase of Paracoccus denitrificans was shown to be very similar to the enzyme of Pseudomonas sp, M. 27. The K _m value for methanol with excess activator (ammonium ions) is 35 M. The pH optimum for enzyme activity with 2,6-dichlorophe-nolindophenol as electronacceptor was at 9.0 A CO-binding type of cytochrome c was present only in cells grown with methanol as carbon and energy source.It has been shown that methanol-oxidation involves electron-transport via cytochrome c and an a-type cytochrome to oxygen. Antimycin A did not inhibit this electron transport and 90% inhibition was obtained by 375 M potassium cyanide. Electron transport from endogenous substrates is possible via cytochrome b and possibly cytochrome o to oxygen. Potassium cyanide inhibited 90% of the electron transport via this pathway at a concentration of 1.42 mM. Measurement of respiration-driven proton translocation proved that during oxidation of methanol to formaldehyde by oxygen one mole of adenosine triphosphate is synthesized in the site 3 region of the electron transport chain. The H⁺/O value found confirmed the H⁺/site ratio of 3–4 found in heterotrophic grown cells. During electron transport from endogenous substrates to oxygen there is a possible synthesis of 3 moles of adenosine triphosphate.In heterotrophically grown cells electron transfer to oxygen follows almost only the branch of the respiratory chain containing cytochrome o. In methanol-grown cells the pathway via the a-type cytochrome seems more important.Abbreviations DCPIP 2,6-dichlorophenolindophenol - PMS phenazine methosulphate - EPR electron paramagnetic resonance - S.D. standard deviation - ATP adenosine triphosphate     

Modeling of microbial substrate conversion,growth and product formation in a recycling fermentor

Paracoccus denitrificans and Bacillus licheniformis were grown in a carbon- and energy source-limited recycling fermentor with 100% biomass feedback. Experimental data for biomass accumulation and product formation as well as rates of carbon dioxide evolution and oxygen consumption were used in a parameter optimization procedure. This procedure was applied on a model which describes biomass growth as a linear function of the substrate consumption rate and the rate of product formation as a linear function of the biomass growth rate. The fitting procedure yielded two growth domains for P. denitrificans. In the first domain the values for the maximal growth yield and the maintenance coefficient were identical to those found in a series of chemostat experiments. The second domain could be described best with linear biomass increase, which is equal to a constant growth yield. Experimental data of a protease producing B. licheniformis also yielded two growth domains via the fitting procedure. Again, in the first domain, maximal growth yield and maintenance requirements were not significantly different from those derived from a series of chemostat experiments. Domain 2 behaviour was different from that observed with P. denitrificans. Product formation halts and more glucose becomes available for biomass formation, and consequently the specific growth rate increases in the shift from domain 1 to 2. It is concluded that for many industrial production processes, it is important to select organisms on the basis of a low maintenance coefficient and a high basic production of the desired product. It seems less important that the maximal production becomes optimized, which is the basis of most selection procedures.     

Molar growth yields,respiration and cytochrome profiles of Beneckea natriegens when grown under carbon limitation in a chemostat

The effect of growth rate on the physiology of Beneckea natriegens was studied in chemostat culture. The molar growth yields (Y) from glucose and oxygen, the specific rates of oxygen (q _{O 2}) and glucose (q _glc) consumption and the specific rate of CO₂ production (q _{CO 2}) were linearly dependent on the growth rate over the dilution rate 0.17 h^-1 to 0.60 h^-1. Further increase in the dilution rate resulted in a decrease in growth yield and respiration rate and these changes were coincident with increases in the specific rate of glucose utilisation and of acetate production. The affinity of Beneckea natriegens for glucose was similar when measured either directly in chemostat culture or in a closed oxygen electrode system using harvested bacteria. The total content of cytochromes decreased with increasing growth rate. However, the quantity of CO-binding cytochromes remained independent of growth rate and correlated with the potential respiration rate.     

Growth yield of denitrifiers using nitrous oxide as a terminal electron acceptor

The molar yields (g cell/mol) forAlcaligenes faecalis, Pseudomonas stutzeri, Paracoccus denitrificans andPseudomonas perfectomarinus batch cultures, under nitrous oxide (N₂O) as the electron acceptor, were 11.2, 8.2, 6.1 and 4.4, respectively.Paracoccus denitrificans andPseudomonas perfectomarinus, which had the slowest growth rates, gave the lowest yields. Large maintenance energy costs may be partially responsible for this. The growth efficiencies ofA. faecalis andPs. perfectomarinus on N₂O indicate that the numbers of sites for oxidative phosphorylation in the electron transport system associated with N₂O reduction are about 49% and 39% of those in the electron transport system associated with O₂ respiration, respectively.     

Energy conservation during nitrate respiration in Paracoccus denitrificans

P/2e ratios were calculated from anaerobic chemostat cultures of Paracoccus denitrificans with nitrogenous oxides as electron acceptor. P/2e ratios were calculated, using the Y _ATP ^max values determined for aerobic cultures. When succinate was the carbon and energy source the average P/2e values of the sulphate-and succinate-limited cultures with nitrate as electron acceptor were 0.5 and 0.7, respectively, and of the nitrite-limited culture 0.9. With gluconate as carbon and energy source the average P/2e values of the gluconate-limited with nitrate as electron acceptor and nitrate limited cultures were 0.9 and 1.1, respectively.H⁺/O ratios measured in cells obtained from sulphate-, succinate, nitrite-, gluconate-and nitratelimited cultures yielded respective average values of 3.4, 4.5, 3.5, 4.8 and 6.2 for endogenous substrates. From our data we conclude that sulphate-and nitritelimitation causes the loss of site I phosphorylation. Nitrite has no influence on the maximum growth yield on ATP. We propose that metabolism in heterotrophically grown cells of Paracoccus dentrificans is regulated on the level of phosphorylation in the site I region of the electron transport chain.     

Regulation of methylammonium transport inParacoccus denitrificans

Depending on the growth conditionsParacoccus denitrificans synthesizes two different carriers mediating uptake of methylamine. When used as a nitrogen source, methylamine is transported via a NH ₄ ⁺ carrier, and its transport is inhibited by NH ₄ ⁺ but not by ethylamine. When used as a carbon source, methylamine is transported by a specific alkylamine carrier, and its transport is inhibited by ethylamine but not by NH ₄ ⁺ . The NH ₄ ⁺ carrier is under nitrogen control, the alkylamine carrier under carbon control.Abbreviations MA Methylamine - FCCP p-trifluormethoxycarbonylcyanide-phenylhydrazone     

Cell yield and bioenergetics of Thiomicrospira denitrificans compared with Thiobacillus denitrificans

From cell yields of Thiomicrospira denitrificans grown in the chemostat at different growth rates under anaerobic conditions a value of 1.4mm S₂O _inf3 ^sup= per g dry wt and per h could be calculated for maintenance energy requirements, and of 5.65 g dry wt per mole S₂O _inf3 ^sup= for the true growth yield.Cell yields of Thiomicrospira denitrificans appeared to be almost half of those of Thiobacillus denitrificans. Though in Thiobacillus denitrificans at D=0.03 h^-1 under anaerobic conditions a value was found of 11.60 g dry wt per mole of thiosulphate used for energetic purposes, a value of 5.72 g dry wt per mole of thiosulphate was found under comparable conditions in Thiomicrospira denitrificans. Under aerobic conditions at D=0.03 h^-1 values of 18.54 g dry wt per mole of thiosulphate were found in Thiobacillus denitrificans whereas Thiomicrospira denitrificans yielded only 9.38 g dry wt per mole of thiosulphate.As in Thiobacillus denitrificans anaerobic cell yields on sulphide were comparable to those on thiosulphate.Calculations have been made which indicate that the biosynthetic efficiency of Thiomicrospira denitrificans is lower than that of Thiobacillus denitrificans. This can only partly be explained by the absence of adenosine-phosphosulphate (APS) reductase.     

Regulatory flexibility of methylotrophic yeasts in chemostat cultures: Simultaneous assimilation of glucose and methanol at a fixed dilution rate

The influence of the composition of methanol/glucose-mixtures as only sources of carbon and energy on growth and regulation of the synthesis of enzymes involved in methanol-dissimilation was studied under chemostat conditions at a fixed dilution rate with the methylotrophic yeasts Hansenula polymorpha and Kloeckera sp. 2201. Both carbon sources were found to be utilized completely independently of the composition of the C₁/C₆ mixture. Using mixtures of ¹⁴C-labelled methanol and glucose the growth yield for glucose was found to be constant for all C₁/C₆-mixtures tested and both yeasts. The growth yield for methanol, however, was reduced by up to 25% when the proportion of methanol in the inflowing medium was lower than 20% (w/w with respect to glucose) for H. polymorpha and 50% (w/w with respect to glucose) for Kloeckera sp. 2201 respectively. During growth with C₁/C₆-mixtures containing higher C₁-proportions of methanol regular growth yields for methanol were recorded which corresponded to the growth yields found with methanol as the only carbon source.The regulation of the synthesis of the enzymes of the dissimilatory pathway for methanol was found to be under multiple control. Although glucose was present in the medium methanol had a positive effect on the synthesis of these enzymes. Thus, in addition to derepression induction by methanol was also observed. This inductive effect was found to increase with increasing proportions of methanol in the mixture. Depending on the enzyme, 10–40% methanol in the mixture resulted in a maximal induction with enzyme specific activities equal to those found in cells grown with methanol as the only carbon source. No further enhancements in enzyme specific activities were observed during growth on mixtures containing more than 40% methanol.Abbreviations and terms C₁ Methanol - C₆ glucose - C₁/C₆ mixture compositions are given in % (w/w) - C₀ concentration of ¹⁴C in the inflowing medium (DPM ml^-1) - C(t) concentration of ¹⁴C incorporated in cells as a function of time t (DPM ml^-1) - d dilution rate (h^-1) - DPM disintegrations per minute - q _s q _C1 and q _C6 are specific rates of consumption of substrate, methanol and glucose respectively [g (g cell dry weight)^-1 h^-1] - q _O2 and q _CO2 are the specific rates of oxygen consumption and carbon dioxide release [mmol (g cell dry weight)^-1 h^-1] - RQ respiration quotient (q _CO2 q _O2 ^-1) - s _C1 and s _C6 are the residual concentrations of methanol and glucose in the culture liquid (g l^-1) - s _O/C1 and s _O/C6 are the concentrations of methanol and glucose in the inflowing medium (g l^-1) - Sp.A. enzyme specific activity - x cell dry weight concentration (g l^-1) - Y _X/C1 and Y _X/C6 are growth yields on methanol and glucose respectively (g cell dry weight (g substrate)^-1 - Y _C/C1 growth yield with methanol with respect to carbon (g carbon assimilated (g carbon supplied)^-1 - _m maximum specific growth rate (h^-1)     

Mixed substrate growth of methylotrophic yeasts in chemostat culture: Influence of the dilution rate on the utilisation of a mixture of glucose and methanol

The growth of Hansenula polymorpha and Kloeckera sp. 2201 with a mixture of glucose and methanol (38.8%/61.2%, w/w) and the regulation of the methanol dissimilating enzymes alcohol oxidase, catalase, formaldehyde dehydrogenase and formate dehydrogenase were studied in chemostat culture, as a function of the dilution rate. Both organisms utilized and assimilated glucose and methanol simultaneously up to dilution rates of 0.30 h^-1 (H. polymorpha) and 0.26h^-1, respectively (Kloeckera sp. 2201) which significantly exceeded _max found for the two yeasts with methanol as the only source of carbon. At higher dilution rates methanol utilisation ceased and only glucose was assimilated. Over the whole range of mixed-substrate growth both carbon sources were assimilated with the same efficiency as during growth with glucose or methanol alone.In cultures of H. polymorpha, however, the growth yield for glucose was lowered by the unmetabolized methanol at high dilution rates. During growth on both carbon sources the repression of the synthesis of all catabolic methanol enzymes which is normally caused by glucose was overcome by the inductive effect of the simultaneously fed methanol. In both organisms the synthesis of alcohol oxidase was found to be regulated differently as compared to catalase, formaldehyde and formate dehydrogenase. Whereas increasing repression of the synthesis of alcohol oxidase was found with increasing dilution rates as indicated by gradually decreasing specific activities of this enzyme in cell-free extracts, the specific activities of this enzyme in cell-free extracts, the specific activities of catalase and the dehydrogenases increased with increasing growth rates until repression started. The results indicate similar patterns of the regulation of the synthesis of methanol dissimilating enzymes in different methylotrophic yeasts.Abbreviations and Terms C₁ Methanol - C₆ glucose; D dilution rate (h^-1) - D _c critical dilution rate (h^-1) - q _s specific, rate of substrate consumption (g substrate [g cell dry weight]^-1 h^-1) - q _CO2 and q _O2 are the specific rates of carbon dioxide release and oxygen consumption (mmol [g cell dry weight]^-1 h^-1) - RQ respiration quotient (q _CO2 q _O2 ¹ ) - s ₀(C₁) and s ₀(C₆) are the concentrations of methanol and glucose in the inflowing medium (g l^-1) - s residual substrate concentration in the culture liquid (g l^-1) - Sp. A. enzyme specific activity - x cell dry weight concentration (gl^-1) - Y _X/C6 growth yield on glucose (g cell dry weight [g substrate]^-1     

Biodegradation of Isopropanol by a Solvent-Tolerant Paracoccus denitrificans Strain

The biodegradation of high concentration isopropanol (2-propanol, IPA) at 16 g/L was investigated by a solvent-tolerant strain of bacteria identified as Paracoccus denitrificans for the first time by 16S rDNA gene sequencing. The strain P. denitrificans GH3 was able to utilize the high concentration of IPA as the sole carbon source within a minimal salts medium with a cell density of 1.5 × 10⁸ cells/mL. The optimal conditions were found as follows: initial pH 7.0, incubation temperature 30°C, with IPA concentration 8 g/L. Under the optimal conditions, strain GH3 utilized 90.3% of IPA in 7 days. Acetone, the major intermediate of aerobic IPA biodegradation, was also monitored as an indicator of microbial IPA utilization. Both IPA and acetone were completely removed from the medium following 216 hr and 240 hr, respectively. The growth of strain GH3 on IPA as a sole carbon and energy source was well described by the Andrews model with a maximum growth rate (μ _max ) = 0.0277/hr, a saturation constant (K _S ) = 0.7333 g/L, and an inhibition concentration (Ki) = 8.9887 g/L. Paracoccus denitrificans GH3 is considered to be well used in degrading IPA in wastewater.     

Growth and physiology of potassium-limited chemostat cultures of Paracoccus denitrificans

In potassium-limited chemostat cultures of Paracoccus denitrificans the maximum specific growth rate (µ_max) was found to depend on the input potassium concentration: At 0.21mM µ_max was 0.10–0.11 h^-1; at 0.44 mM 0.15–0.16 h^-1 and at 0.66 mM 0.20–0.21 h^-1. The plots of the specific rates of oxygen-, succinate-and potassium consumption against gave straight lines. The intracellular potassium concentration was a linear function of and varied from 1% (0.13 M) at a value of 0.034 h^-1 to 2.2% (0.29 M) at =0.26 h^-1; the potassium concentration gradient and the potassium concentration in the culture fluid in the steady state were dependent on the input potassium concentration. The potassium concentration gradient varied from 8,900-1,200. At all values 20–25% of the total energy production was used for potassium transport. 350,100 and 30 ATP molecules were calculated to be required to maintain one potassium ion intracellular during 1 h at values of 0.034, 0.197 and 0.257 h^-1 respectively. It is concluded that the amount of circulation of potassium is dependent on the potassium concentration gradient or on the potassium concentration in the culture in the steady state. The dependency of µ_max on the input potassium concentration was explained by the assumption that at low input potassium concentrations the net uptake of potassium (influx-efflux) is not rapidly enough to maintain the high potassium gradient in the existing cells and to establish it in the newly formed cells. At high values and at high input potassium concentrations µ_max is limited by the specific rate of oxygen consumption, which was found to be 11–12 mmol O₂ g dry weight^-1 h^-1 at µ_max for potassium-, succinate-and sulphate-limited chemostat cultures.     

Reconsideration of the efficiency of energy transduction in Paracoccus denitrificans during growth under a variety of culture conditions

1. Theoretical overall P/2e^- ratios were calculated for growth of Paracoccus denitrificans under a variety of culture conditions on the basis of a growth model and recently published schemes of electron transport and associated proton translocation. 2. Experimental overall P/2e^- ratios were calculated, using the specific rate of ATP synthesis determined in cultures grown under aerobic carbon source-limited conditions. 3. The experimental P/2e^- was equal to the theoretical P/2e^- for aerobic sulphate-limited growth with gluconate or succinate as carbon source, on the assumption that site 1 phosphorylation was completely absent. 4. The experimental and the theoretical P/2e^- were similar for growth on nitrate as terminal electron acceptor and gluconate, mannitol or succinate as carbon source, on the assumption that nitrate enters the cell via the electroneutral nitrate-nitrite antiport system. 5. The experimental and theoretical P/2e^- were similar for growth on nitrite as terminal electron acceptor and mannitol or succinate as carbon source. 6. The experimental P/2e^- was substantially lower than the theoretical P/2e^- for aerobic growth with nitrate as nitrogen source and gluconate or mannitol as carbon source. The amount of energy needed for assimilative reduction of nitrate to ammonia was calculated from this difference.Dedicated to Prof. H. G. Schlegel on the occasion of his 60th birthday     

Microbial treatment of a synthetic sour brine

Summary The ability of the chemoautotroph and facultative anaerobeThiobacillus denitrificans to deodorize and detoxify an oil-field-produced water containing sulphides was evaluated under simulated field conditions. A sulphide-tolerant strain ofT. denitrificans was used to remove inorganic sulphide from a synthetic sour brine containing 4000 mg L^–1 total dissolved solids (TDS) and 100 mg L^–1 sulphide. The sour brine was treated continuously in a rectangular plugflow reactor which approximated the scaled dimensions of an existing field detention pond. The head space of the reactor was purged with N₂ in order to capture H₂S off-gases in a zinc acetate trap. Brine was fed to the reactor continuously for 90 days at rates corresponding to residence times of 0.17–6 days. Temperature and pH ranged from 22 to 40.5°C and 7.5 to 8.8, respectively. The start-up biomass concentration was approximately 100 mg L^–1 (by dry weight). No. additionalT. denitrificans biomass was added to the reactor after start-up. At residence times of 0.3 days and greater inorganic sulphide was undetectable in the effuent. No H₂S was detected in the outlet gas or the zinc acetate trap. Approximately 80% of the sulphide feed was oxidized to sulphate and removed from the reactor in the liquid effluent. The remainder was partially oxidized to elemental sulphur which was retained in the reactor. It is suggested that oxidation of inorganic sulphides byT. denitrificans represents a viable process concept for the treatment of sour water co-produced with oil and gas.     

Simultaneous utilization of methanol and glucose by Hansenula polymorpha (Torulopsis sp.) MH 26, a chemostatic investigation on the distribution of 14C-methanol

Simultaneous utilization of methanol and glucose by Hansenula polymorpha (Torulopsis sp.) MH 26 results in an increase in growth yield of up to 18% in dependence of the mixing proportion. The distribution of carbon from ¹⁴C-methanol into biomass and carbon dioxide was investigated. The distribution pattern was strongly influenced by the mixing proportion showing that methanol plays an increasing role as an energy donor as the glucose content in the mixture increased. Due to these data and verified by theoretical considerations the effect on growth yield was discussed to be caused by an interconnection in the conversion of the individual substrates. This is attributed to glucose delivering the acceptor for C₁-assimilation and resulting in a more efficient utilization of glucose carbon on the one as well as the energy content of methanol on the other hand.     

Impact of light/dark regimen on growth rate,biomass formation and bacteriochlorophyll synthesis in Erythromicrobium hydrolyticum

The impact of illumination on specific growth rate, biomass formation, and synthesis of photopigment was studied in Erythromicrobium hydrolyticum, an obligately aerobic heterotrophic bacterium having the ability to synthesize bacteriochlorophyll a. In dark-grown continuous cultures the concentration of protein increased with increasing dilution rate, the concentration of bacteriochlorophyll a showed the opposite effect. At a dilution rate of 0.08 h^-1 (68% of _max in the dark) and S_R-acetate of 11.8 mM, the concentration of BChla of illuminated cultures in steady-state was 11–22 nM, compared to 230–241 nM in cultures incubated in darkness. No significant differences were observed in the concentration of protein. A shift from darkness to light conditions resulted in increased specific growth rates resulting in increased biomass formation, thus showing that light enhances growth by serving as an additional energy source. This phenomenon, however, was temporary because bacteriochlorophyll synthesis is inhibited by light. In contrast to incubation in continuous light or dark, incubation under light/dark regimen resulted in permanently enhanced biomass formation. In the dark periods, bacteriochlorophyll was synthesized at elevated rates (compared to constant darkness), thus compensating the inhibitory effect of light in the preceding period. It thus appears that the organism is well-adpated to life in environments with alternating light/dark conditions. The ecological relevance of the observations is discussed.Non-standard abbreviations BChla bacteriochlorophyll a - D dilution rate - spceific growth rate - K_s saturation constant - S_R concentration of limiting in inflowing medium of chemostat     

Study of purine degradation in aqueous solutions byParacoccus denitrificans

In this study the degradation of extracellular purines by the bacteriumParacoccus denitrificans was examined with aqueous purine solutions.Paracoccus denitrificans was able to decompose free purine bases and 5-mononucleotides. The nitrogen-containing products of the degradation were ammonia and urea. Purine uptake was the main control of purine decomposition. In the cases of guanine, xanthine, hypoxanthine, and urate, further control was exerted by induction. Furthermore, the uptake of the purines caused differences in the duration and temporal development of the substrate degration. It was also responsible for the inhibitory effects of the purines on the decomposition of one another when the substrates were used in mixtures. Also, fermentation parameters like biomass and purine concentration, pH, and temperature influenced the purine usage ofParacoccus denitrificans.     

Growth kinetics and Pho84 phosphate transporter activity of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> under phosphate-limited conditions

The effect of phosphate (P _i ) concentration on the growth behavior of Saccharomyces cerevisiae strain CEN.PK113-5D in phosphate-limited batch and chemostat cultures was studied. The range of dilution rates used in the present study was 0.08–0.45 h⁻¹. The batch growth of yeast cells followed Monod relationship, but growth of the cells in phosphate-limited chemostat showed change in growth kinetics with increasing dilution rates. The difference in growth kinetics of the yeast cells in phosphate-limited chemostat for dilution rates below and above approximately 0.2 h⁻¹ has been discussed in terms of the batch growth kinetic data and the change in the metabolic activity of the yeast cells. Immunological detection of a C-terminally myc epitope-tagged Pho84 fusion protein indicated derepressive expression of the Pho84 high-affinity P _i transporter in the entire range of dilution rates employed in this study. Phosphate transport activity mediated by Pho84 transporter was highest at very low dilution rates, i.e. 0.08–0.1 h⁻¹, corresponding to conditions in which the amount of synthesized Pho84 was at its maximum.     

A continuous culture study of the bioenergetic aspects of growth and production of exocellular protease in Bacillus licheniformis

Summary Bacillus licheniformis S 1684 is able to produce an alkaline serine protease exocellularly. In glucose-limited chemostat cultures the specific rate of protease production was maximal at a -value of 0.22. Above this growth rate protease production was repressed. Dependent on 10–20% of the glucose input was used for exocellular product formation. The degree of reduction of exocellular products was 4.1.Maximum molar growth yields were high and indicate a high efficiency of growth. The values of Y _glu ^max and YO ₂ ^max were 83.8 and 53.3, respectively. When Y _glu ^max was corrected for the amount of glucose used for product formation a value of 100.3 was obtained. These high maximum molar growth yields are most probably caused by a high Y _ATP ^max . Anaerobic batch experiments showed a Y _ATP of 14.6.Sometimes the used strain was instable in cell morphology and protease production. Non-protease producing cells most probably develop from producing cells by mutation in the rel-gene. Producing cells most probably are relaxed (rel ^-) and non-producing cells stringent (rel ⁺).Glossary specific growth rate (h^-1) - Y _sub growth yield permol substrate (g biomass/mol) - Y ^max maximum molar growth yield, corrected for maintenance requirements (g biomass/mol) - Y ^max(corr) Y ^max corrected for product formation (g biomass/mol) - m _sub maintenance requirements (mol/g biomass·h) - m _sub(corr) maintenance requirements corrected for product formation (mol/g biomass·h) - Y _c fraction of organic substrate converted in biomass - z fraction of organic substrate converted in exocellular products - d fraction of organic substrate converted in CO₂ (g mol/g atom C) - Crec% carbon recovery % - average degree of reduction of exocellular products - P/O amount of ATP produced during electron-transport of 2 electrons to oxygen     

Function of terminal acceptors in the biosynthesis of denitrification pathway components inParacoccus denitrificans

Limited aeration of cell suspension in growth medium was used to study the kinetics of formation of nitrite reductase and nitrous-oxide reductase and their physiological electron donor, cytochromec-550, during the anaerobic adaptation ofParacoccus denitrificans. The crucial step in the regulation of synthesis of these components is the repressive effect of oxygen while nitrogenous acceptors (NO₃ ⁻, NO₂ ⁻, N₂O) probably play no role as inducers. The time course of the enzyme activites was analogous (after a lag phase a sharp increase with a maximum after 3 h) and differed from the kinetics of synthesis of cytochromec-550 (gradual rise throughout the 8-h experiment).