Gas Exchange of Algae: II. Effects of Oxygen, Helium, and Argon on the Photosynthesis of Chlorella pyrenoidosa

Changes in the oxygen partial pressure of air over the range of 8 to 258 mm of Hg did not adversely affect the photosynthetic capacity of Chlorella pyrenoidosa. Gas exchange and growth measurements remained constant for 3-week periods and were similar to air controls (oxygen pressure of 160 mm of Hg). Oxygen partial pressures of 532 and 745 mm of Hg had an adverse effect on algal metabolism. Carbon dioxide consumption was 24% lower in the gas mixture containing oxygen at a pressure 532 mm of Hg than in the air control, and the growth rate was slightly reduced. Oxygen at a partial pressure of 745 mm of Hg decreased the photosynthetic rate 39% and the growth rate 37% over the corresponding rates in air. The lowered metabolic rates remained constant during 14 days of measurements, and the effect was reversible after this time. Substitution of helium or argon for the nitrogen in air had no effect on oxygen production, carbon dioxide consumption, or growth rate for 3-week periods. All measurements were made at a total pressure of 760 mm of Hg, and all gas mixtures were enriched with 2% carbon dioxide. Thus, the physiological functioning and reliability of a photosynthetic gas exchanger should not be adversely affected by: (i) oxygen partial pressures ranging from 8 to 258 mm of Hg; (ii) the use of pure oxygen at reduced total pressure (155 to 258 mm of Hg) unless pressure per se affects photosynthesis, or (iii) the inclusion of helium or argon in the gas environment (up to a partial pressure of 595 mm of Hg).     

Effect of elevated dissolved carbon dioxide concentrations on growth of Corynebacterium glutamicum on D-glucose and L-lactate

The effect of increased dissolved carbon dioxide concentrations on growth of Corynebacterium glutamicum was studied with continuous turbidostatic cultures. The carbon sources were either l-lactate or d-glucose. To increase the dissolved carbon dioxide concentration the carbon dioxide partial pressure of the inlet gas stream pCO2,IN was increased stepwise from 0.0003 bar (air) up to 0.79 bar, while the oxygen partial pressure of the inlet gas stream was kept constant at 0.21 bar. For each resulting carbon dioxide partial pressure pCO2 the maximum specific growth rate mu(max) was determined from the feed rate resulting from the turbidostatic control. On d-glucose and pCO2 up to 0.26 bar, mu(max) was mostly constant around 0.58 h(-1). Higher pCO2 led to a slight decrease of mu(max). On l-lactate mu(max) increased gradually with increasing carbon dioxide partial pressures from 0.37 h(-1) under aeration with air to a maximum value of 0.47 h(-1) at a pCO2 of 0.26 bar. At very high pCO2 (0.81 bar) mu(max) decreased down to 0.35 h(-1) independent of the carbon source.     

Growth and beta-galactosidase activity in cultures of Kluyveromyces marxianus under increased air pressure

AIMS: To investigate the effect of total air pressure raise on cell growth and intracellular beta-galactosidase activity in batch cultures of Kluyveromyces marxianus CBS 7894. METHODS AND RESULTS: A pressurized bioreactor was used for K. marxianus batch cultivation under increased air pressure from 1.2 to 6 bar. Under these conditions no inhibition of cell growth was observed. Moreover, the improvement of the oxygen transfer rate (OTR) from the gas to the culture medium by pressurization led to an enhancement of the cell growth rate obtained at atmospheric pressure without aeration. The specific beta-galactosidase productivity increased from 5.8 to 17.0 U gCD-1 h-1 using a 6-bar air pressure instead of air at atmospheric pressure. The antioxidant enzyme superoxide dismutase (SOD) was slightly induced by the air pressure raise, which indicates that the defensive mechanisms of the cells can cope with an air pressure up to 6 bar. CONCLUSIONS: These experiments showed that the increase of air pressure up to 6 bar is an alternative to other methods of preventing the oxygen limitation and can be applied in the beta-galactosidase production by K. marxianus. SIGNIFICANCE AND IMPACT OF THE STUDY: The results here reported proved that, in what biological aspects are concerned, it is possible to use the air pressure increase as an optimization parameter of beta-galactosidase production in high-density cell cultures of K. marxianus strains.     

Fed-batch cultivation of Saccharomyces cerevisiae in a hyperbaric bioreactor

Fed-batch is the dominating mode of operation in high-cell-density cultures of Saccharomyces cerevisae in processes such as the production of baker's yeast and recombinant proteins, where the high oxygen demand of these cultures makes its supply an important and difficult task. The aim of this work was to study the use of hyperbaric air for oxygen mass transfer improvement on S. cerevisiae fed-batch cultivation. The effects of increased air pressure up to 1.5 MPa on cell behavior were investigated. The effects of oxygen and carbon dioxide were dissociated from the effects of total pressure by the use of pure oxygen and gas mixtures enriched with CO(2). Fed-batch experiments were performed in a stirred tank reactor with a 600 mL stainless steel vessel. An exponential feeding profile at dilution rates up to 0.1 h(-)(1) was used in order to ensure a subcritical flux of substrate and, consequently, to prevent ethanol formation due to glucose excess. The ethanol production observed at atmospheric pressure was reduced by the bioreactor pressurization up to 1.0 MPa. The maximum biomass yield, 0.5 g g(-)(1) (cell mass produced per mass of glucose consumed) was attained whenever pressure was increased gradually through time. This demonstrates the adaptive behavior of the cells to the hyperbaric conditions. This work proved that hyperbaric air up to 1.0 MPa (0.2 MPa of oxygen partial pressure) could be applied to S. cerevisiae cultivation under low glucose flux. Above that critical oxygen partial pressure value, i.e., for oxygen pressures of 0.32 and 0.5 MPa, a drastic cell growth inhibition and viability loss were observed. The increase of carbon dioxide partial pressure in the gas mixture up to 48 kPa slightly decreased the overall cell mass yield but had negligible effects on cell viability.     

Effects of controlled gas environments in solid-substrate fermentations of rice

The gas environment is solid-substrate fermentations of rice significantly affected levels of biomass and enzyme formation by a fungal species screened for high amylase production. Constant oxygen and carbon dioxide partial pressures were maintained at various levels in fermentations by Aspergillus oryzae. Control of the gas phase was maintained by a “static” aeration system admitting oxygen on demand and stripping excess carbon dioxide during fermentation. Constant water vapor pressures were also maintained by means of saturated salt solutions. High Oxygen pressures stimulated amylase productivity significantly. On the other hand, amylase production was severely inhibited at high carbon dioxide pressures. While relatively insensitive to oxygen pressure, maximum biomass productivities were obtained at an intermediate carbon dioxide pressure. High oxygen transfer rates were obtained at elevated oxygen pressures, suggesting, in view of the stimulatory effect of oxygen on amylase production, a stringent oxygen requirement for enzyme synthesis. Solid-substrate fermentations were highly advantageous as compared with submerged cultures in similar gas environments. Not only were amylase productivities significantly higher, but the enzyme was highly concentration in the aqueous phase of the semisolid substrate particles and could be extracted in a small volume of liquid. Results of this work suggest that biomass and product formation in microbial processes may be amenable to control by the gas environment. This is believed to offer an interesting potential for optimizing selected industrial fermentation processes with respect to productivity and energy consumption.     

Characterization and improvement of oxygen transfer in pilot plant external air-lift bioreactor for mycelial biomass production

The oxygen transfer dynamics in a pilot plant external air-lift bioreactor (EALB) during the cultivation of mycelial biomass were characterized with respect to hydrodynamic parameters of gas holdup (), oxygen transfer coefficient (K_La) and superficial gas velocity (U _g), and dissolved oxygen (DO). An increased flow rate of air supply was required to meet the increased oxygen demand with mycelial biomass growth. Consequently, an increase in air flow rate led to an increase in , K_La and the DO level. The enhancement of oxygen transfer rate in the cultivated broth system, however, was limited with highly increased viscosity of the mycelial broth. An increase in air flow rate from 1.25 to 2.00 v/v/m resulted in a low increment of oxygen transfer. The newly designed pilot plant EALB with two air spargers significantly improved processing reliability, aeration rate and K_La. The pilot plant EALB process, operated under a top pressure from 0 to 1.0 bars, also demonstrated a significant improvement of oxygenation efficiency by more than 20% in DO and K_La. The performance of the two sparger EALB process under top pressure demonstrated an efficient and economical aerobic system with fast mycelial growth and high biomass productivity in mycelial biomass production and wastewater treatment.     

Air pressure effects on biomass yield of two different Kluyveromyces strains

The use of air pressure as a way of improving oxygen transfer in aerobic bioreactors was investigated. To compare the air pressure effects with traditional air bubbled cultures, experiments using a pressure reactor and a stirred flask, with the same oxygen transfer rate, were made. Kluyveromyces marxianus is an important industrial yeast and some of it show a “Kluyver effect” for lactose: even under oxygen limited growth conditions, certain disaccharides that support aerobic, respiratory growth, are not fermented. This study deals with the effect of increased pressure on the physiological behavior of two Kluyveromyces strains: K. marxianus ATCC10022 is a lactose-fermenting strain, whereas K. marxianus CBS 7894 has a Kluyver-effect for lactose. For K. marxianus ATCC10022 an air pressure increase of 2 bar led to a 3-fold increase in biomass yield. When air pressure increased an enhancement of ethanol oxidation of cell yeasts was also observed. Batch cultures of K. marxianus CBS 7894 exhibited different growth behaviour. Its metabolism was always oxidative and ethanol was never produced. With the increase in air pressure, it was possible to increase the productivity in biomass of K. marxianus CBS 7894. As a response to high oxygen concentrations, due to the increase in oxygen partial pressure, oxidative stress in the cells was also studied. Antioxidant defences, such as superoxide dismutase, catalase, and glutathione reductase, were at high activity levels, suggesting that these yeast strains could tolerate the increased pressures applied.     

Application of Oxygen-Enriched Aeration in the Conversion of Glycerol to Dihydroxyacetone by Gluconobacter melanogenus IFO 3293

Gluconobacter melanogenus 3293 converts glycerol to dihydroxyacetone(DHA) during exponential growth on a yeast extract-phosphate medium at pH 7. The efficiency of this conversion in 25-liter batch fermentations has been found to increase over threefold, when oxygen tension is controlled by increasing the partial pressure of oxygen in the aeration. Conversion of glycerol to DHA does not occur under oxygen-limited fermentation conditions. When the dissolved oxygen tension was maintained at 0.05 atmospheres (using oxygen-enriched air), quantitative conversion of up to 100 g of glycerol/liter to DHA was obtained in 33 h. The amount of glycerol converted can be increased without increasing impeller speed or aeration rate. This increase is not the result of increased production of cell mass. The specific conversion of glycerol to DHA increased from 12.2 g of DHA/g of cell mass at the point of maximum conversion to 35.8 with oxygen enrichment. This increased specific production occurred even though the specific growth rate during the period of oxygen enrichment decreased from 0.23 to 0.06/h.     

Batch and fed-batch cultures of E. coli TB1 at different oxygen transfer rates

Batch cultures of E. coli TB1/pUC13 were carried out at different oxygen transfer rates (OTR) enhanced by the increase of stirring rate and by the increase of air total pressure of the bioreactor. These two variables showed to have little effect on cell growth but a negative effect on cytochrome b5 (recombinant protein) production. However, this effect was more significant of high stirring rates than for values of pressure up to 0.4?MPa. The effects of stirring and pressure were also investigated for fed-batch mode operation. In this type of cell cultivation high cell densities are reached, thus a high capacity of oxygen supply of the system is required. To compare the two ways of improving OTR, cell behaviour was followed in two bioreactors at different operational conditions giving the same maximum OTR value. The first one operated at a high stirring rate (500?rpm) and at atmospheric pressure (0.1?MPa) and the other one at high air pressure (0.48?MPa) and low stirring rate. The increased pressure seemed to be a better way of ensuring an adequate oxygen supply to a culture of E. coli TB1 cells than an increased stirring rate. For the high pressure experiment a higher cellular density was reached, as well as a higher cyt.b5 expression which led to a 4-fold increase in final productivity. These experiments showed that bioreactor pressurization can be successfully used as a means of enhancing oxygen mass transfer to shear sensitive cell cultures.     

Synthesis of staphylococcal enterotoxin A and nuclease under controlled fermentor conditions.

The production of enterotoxin A and nuclease by Staphylococcus aureus strain 100 was studied in a 1.0-liter fermentor. The effects of the gas flow rate, pH, and dissolved oxygen were evaluated. Toxin and nuclease secretion occurred under all conditions which permitted growth of the organism. Final yields of toxin and nuclease in cultures grown at constant air flow rates, ranging from 50 to 500 cm3 per min, were higher at successively higher flow rates. An optimum flow rate for either toxin or nuclease production was not observed. When the aeration rate alone or aeration rate and pH were held constant, the dissolved oxygen levels in the culture decreased from the initial 100% level to 0 to 5% 3 to 4 h after inoculation. The O2 demand of the culture then maintained this level for an additional 4 to 5 h. This low dissolved oxygen interval was characterized by rapid growth and extracellular protein production. Controlling the dissolved oxygen at a constant level throughout growth did not increase the final levels of toxin and nuclease above those achieved at the respective constant pH values. Growth under the influence of a constant aeration rate of 500 cm3 per min and a constant pH of 6.5 and 7.0 yielded the highest titers of nuclease (1,550 units/ml) and toxin (10.5 mug/ml) obtained in any of the fermentations conducted in this study. Sparging fermentor cultures with pure oxygen at a rate of 100 cm3 per min yielded growth and extracellular protein levels similar to those achieved at the sparge rate of 500 cm3 of air per min. Controlling the dissolved oxygen at 100% of pure oxygen saturation appeared to inhibit the culture, as the final cultural turbidity as well as the levels of toxin and nuclease were reduced. These data indicate that enterotoxin and nuclease secretions are closely associated with the growth of strain 100. Analyses of the production rates of these components indicated that early log phase was the most efficient production interval in the growth cycle and that this efficiency was increased by pH control at 6.7 to 6.8 and dissolved oxygen control at 10% of air saturation.     

Synthesis of staphylococcal enterotoxin A and nuclease under controlled fermentor conditions.

The production of enterotoxin A and nuclease by Staphylococcus aureus strain 100 was studied in a 1.0-liter fermentor. The effects of the gas flow rate, pH, and dissolved oxygen were evaluated. Toxin and nuclease secretion occurred under all conditions which permitted growth of the organism. Final yields of toxin and nuclease in cultures grown at constant air flow rates, ranging from 50 to 500 cm3 per min, were higher at successively higher flow rates. An optimum flow rate for either toxin or nuclease production was not observed. When the aeration rate alone or aeration rate and pH were held constant, the dissolved oxygen levels in the culture decreased from the initial 100% level to 0 to 5% 3 to 4 h after inoculation. The O2 demand of the culture then maintained this level for an additional 4 to 5 h. This low dissolved oxygen interval was characterized by rapid growth and extracellular protein production. Controlling the dissolved oxygen at a constant level throughout growth did not increase the final levels of toxin and nuclease above those achieved at the respective constant pH values. Growth under the influence of a constant aeration rate of 500 cm3 per min and a constant pH of 6.5 and 7.0 yielded the highest titers of nuclease (1,550 units/ml) and toxin (10.5 mug/ml) obtained in any of the fermentations conducted in this study. Sparging fermentor cultures with pure oxygen at a rate of 100 cm3 per min yielded growth and extracellular protein levels similar to those achieved at the sparge rate of 500 cm3 of air per min. Controlling the dissolved oxygen at 100% of pure oxygen saturation appeared to inhibit the culture, as the final cultural turbidity as well as the levels of toxin and nuclease were reduced. These data indicate that enterotoxin and nuclease secretions are closely associated with the growth of strain 100. Analyses of the production rates of these components indicated that early log phase was the most efficient production interval in the growth cycle and that this efficiency was increased by pH control at 6.7 to 6.8 and dissolved oxygen control at 10% of air saturation.     

An oxygen supply strategy for the large-scale production of tissue plasminogen activator by microcarrier cell culture

An oxygen supply strategy involving agitation speed and aeration method for the large-scale production of tissue plasminogen activator (TPA) by a microcarrier cell culture was investigated by small-scale model experiments. A preliminary calculation indicated that diffusion limitation of dissolved oxygen (DO) could be caused in a microcarrier sedimentation layer more than 0.5 mm in thickness. Within an agitation speed range above 70 rpm, which was the critical speed for all of the microcarrier beads to remain suspended and thus for avoiding a deficiency of DO, the TPA productivity was higher at a lower agitation speed, while the cell concentration was not affected by the agitation speed. The addition of soluble starch to the culture medium prevented sedimentation of the microcarrier beads, even at the low agitation speed of 20 rpm, resulting in a TPA productivity higher than that at 70 rpm, which was the optimum speed without soluble starch. Use of an air spray system with an optimized air flow rate resulted in a k_La 2.35 times higher than that with simple surface aeration. Increasing the internal pressure of the culture from 0.2 kg/cm² (1209 hPa) to 1.5 kg/cm² (2483 hPa) had no effect on the cell growth but slightly increased the TPA production rates. However, based on the glucose consumption, both the cell and TPA yields were much improved by pressurization. As an optimum mixing and oxygen supply strategy for the production of TPA on a large scale, it is recommended that soluble starch be added to the culture medium to allow the microcarrier suspension to be maintained at a low agitation speed, while keeping a high oxygen transfer rate by means of an air spray system and pressurization.     

Over‐pressurized bioreactors: Application to microbial cell cultures

In industrial biotechnology, microbial cultures are exposed to different local pressures inside bioreactors. Depending on the microbial species and strains, the increased pressure may have detrimental or beneficial effects on cellular growth and product formation. In this review, the effects of increased air pressure on various microbial cultures growing in bioreactors under moderate total pressure conditions (maximum, 15 bar) will be discussed. Recent data illustrating the diversity of increased air pressure effects at different levels in microbial cells cultivation will be presented, with particular attention to the effects of oxygen and carbon dioxide partial pressures on cellular growth and product formation, and the concomitant effect of oxygen pressure on antioxidant cellular defense mechanisms. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:767–775, 2014     

Physiological behaviour of Saccharomyces cerevisiaeunder increased air and oxygen pressures

Saccharomyces cerevisiae, in a pressure batch reactor, coped with higher air (1.2-3 bar) pressures better than with pure oxygen pressures (1.2-3 bar) for an equivalent dissolved oxygen concentration. However, pure oxygen pressure enhanced ethanol production. Both pressures did not influence the type of metabolism followed by the organism which was always oxidoreductive. Growth was inhibited with the increase of air and pure oxygen pressure and almost completely inhibited with 8 bar of pure oxygen. Above 3 bar activities of mitochondrial superoxide dismutase and glutathione reductase increased with air pressure, but cytosolic superoxide dismutase and catalase increased activity only in pure oxygen pressure.     

Carbon dioxide inhibition of yeast growth in biomass production

Saccharomyces cerevisiae was grown under aerobic and substrate-limiting conditions for efficient biomass production. Under these conditions, where the sugar substrate was fed incrementally, the growth pattern of the yeast cells was found to be uniform, as indicated by a constant respiratory quotient during the entire growing period. The effect of carbon dioxide was investigated by replacing portions of the nitrogen in the air stream with carbon dioxide, while maintaining the oxygen content at the normal 20% level, so that identical oxygen transfer rate and atmospheric pressure were maintained for all experiments with different partial pressures of carbon dioxide. Inhibition of yeast growth was negligible below 20% CO₂ in the aeration mixture. Slight inhibition was noted at the 40% CO₂ level and significant inhibition was noted above the 50% CO₂, level, corresponding to 1.6 × 10^?2M of dissolved CO₂ in the fermentor broth. High carbon dioxide content in the gas phase also inhibited the fermentation activity of baker's yeast.     

Effect of PO2 on growth and physiological characteristics of Candida utilis in a multistage tower fermentor

The effect of increasing the partial pressure of oxygen in the aeration gas on growth and physiological activity of the yeast Candida utilis in a multistage tower fermentor was studied. The measurements were made at steady states of continuous culture for single values of dilution rate, temperature, and pH in all stages of the fermentor and with one given ethanol concentration in the growth medium feed. The partial pressure of oxygen in the gas phase was changed in the range from 165 to 310 torr. The results revealed the existence of the upper critical value of the partial oxygen pressure in the gas phase. It was demonstrated that the upper critical value of PO ₂ influences not only the growth rate, biomass yield, and productivity but also the cell physiology resulting in changes of respiration activity and activity of alcohol and aldehyde dehydrogenases.     

Oxidative stress response of <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> to hydrogen peroxide,paraquat and pressure

The aim of this work was to study the oxidative stress response of Kluyveromyces marxianus to hydrogen peroxide (50 mM), paraquat (1 mM), an increase in air pressure (120 kPa, 600 kPa) and pure oxygen pressure (120-600 kPa) in a pressurized bioreactor. The effect of these oxidants on metabolism and on the induction of antioxidant enzymes was investigated. The exposure for 1 h of K. marxianus at exponential growth phase with either H(2)O(2) or paraquat, under air pressure of 120 kPa or 600 kPa, induced an increase in both superoxide dismutase (SOD) and glutathione reductase (GR) content. SOD induction by the chemical oxidants was independent of the air pressure values used. A 2-fold increase in SOD activity was observed after 1 h of exposure to H(2)O(2) and a 3-fold increase was obtained by the presence of paraquat, with both air pressures studied. In contrast, GR activity was raised 1.7-fold by the exposure to both chemicals with 120 kPa, but a 2.4-fold GR induction was obtained with 600 kPa. As opposed to Saccharomyces cerevisiae, catalase was not induced and was even lower than the normal basal levels. This antioxidant enzyme seemed to be inhibited under increasing oxygen partial pressure. The cells showed a significant increase in SOD and GR activity levels, 4.7-fold and 4.4-fold, when exposed for 24 h to 120 kPa pure oxygen pressure. This behaviour was even more patent with 400 kPa. However, whenever cells were previously exposed to low air pressures, low enzymatic activity levels were measured after subsequent exposure to pure oxygen pressure.     

Influence of pressure on growth of Pseudomonas fluorescens

Summary The effect of increased pressure on the growth of the bacterium Pseudomonas fluorescens has been investigated in an airlift-fermenter (10 l) up to 8 bars. It could be established, that increased hydrostatic pressure has a strong effect on the metabolism of the bacterium.     

Effect of multistream ethanol feeding on growth and physiological characteristics of Candida utilis in a multistage tower fermenter

The effect of using a multistream feed for carbon and energy supply on the growth and physiological activity of the yeast Candida utilis in a multistage tower fermenter has been studied. Measurements were made at steady states of continuous culture for single values of dilution rate, temperature and pH in all stages of the fermenter and with the same total ethanol supplied. A comparison of the results obtained with multistream and single-stream ethanol feeds revealed that the type of ethanol feed influences the cell growth rate, rate of ethanol dissimilation, biomass yield, productivity and the cell physiology in the individual stages of the fermenter. Multistream ethanol feeding eliminates the growth inhibition due to insufficient energy production from ethanol oxidation at higher partial pressure of oxygen in the aeration gas. Using the optimal type of ethanol feed, better process parameters for SCP production are achieved.     

The role of the gas phase in the greening and growth of illuminated cell suspension cultures of spinach (Spinacia oleracea,L.)

Summary The gas phase developed above spinach suspension cultures critically affected their growth and greening. Ethylene accumulation inhibited greening; this effect of ethylene was antagonised when the culture gas phase was enriched with carbon dioxide. Greening was enhanced by reducing the partial pressure of oxygen below the air level; this effect was observed when oxygen supply did not restrict growth. One of the authors (C.C.D.) was supported by an S.R.C. studentship grant during this work.