High density cultivation of Anchusa officinalis in a stirred-tank bioreactor with in situ filtration

Previously, Su et al. [Biotechnol Bioeng 42: 884–890 (1993)] reported improved production of rosmarinic acid by Anchusa officinalis in shake-flask cultures using a cultivation strategy that involved intermittent medium exchange. Implementation of this cultivation strategy in 2.5-1 stirred-tank bioreactor cultures is investigated in the present study. Intermittent cell/medium separation in the bioreactor was accomplished by means of automated in situ culture filtration. In the bioreactor culture, rosmarinic acid production was found very sensitive to agitation and aeration conditions as well as dissolved oxygen concentration. A maximum cell density of 35 g dry weight/l and a rosmarinic acid concentration of 3.7 g/l were obtained by maintaining the dissolved oxygen concentration above 30% air saturation, gradually raising the impeller tip speed from 34 cm/s to 72 cm/s, and keeping the aeration rate at 0.44 vvm while increasing the O₂: air ratio in the gas feed stream to 4:1. This result is comparable with the data obtained from shake-flask cultures using the same culture strategy.     

THE ACTIVITY OF YEAST INVERTASE AS A FUNCTION OF OXIDATION-REDUCTION POTENTIAL

The activity of yeast invertase as a function of oxidation-reduction potential has been investigated using a large number of oxidants and reductants. The activity is constant over the range of E_h from –270 to +600 mv., but above E_h = +600 mv. there is a sharp decrease in activity reaching 0 at E_h = +1,000 mv. The inhibiting action of strong oxidants is upon the enzyme rather than on the substrate and appears to be essentially irreversible Experiments indicate that the inhibiting action of strong oxidants on invertase is primarily related to their high oxidation-reduction potential rather than to a specific toxic action unrelated to E_h. The effects of oxidation-reduction potential upon invertase activity are independent of the purity of the enzyme, since they are the same for commercial invertases, fresh bakers'' yeast, powdered bakers'' yeast, brewers'' yeast, and highly purified invertase. Possible mechanisms involved in the inactivation of invertase by oxidants are discussed.     

Effect of partial pressure of CO2 on the production of thermostable α-amylase and neutral protease by Bacillus caldolyticus

Controlling the concentration of dissolved oxygen is a standard feature in aerobic fermentation processes but the measurement of dissolved CO₂ concentrations is often neglected in spite of its influence on the cellular metabolism. In this work room air and room air supplemented with 5 and 10% carbon dioxide were used for aeration during the cultivation of the thermophilic microorganism Bacillus caldolyticus (DSM 405) on starch to produce α-amylase (E.C. 3.2.1.1) and neutral protease (E.C. 3.4.24.27/28). The increased CO₂ concentrations resulted in a 22% raise in activity of secreted α-amylase and a 43% raise in protease activity when compared with aeration with un-supplemented room air. There was no effect on the final biomass concentration. Furthermore, the lag-phase of fermentation was reduced by 30%, further increasing the productivity of α-amylase production. Determinations of dissolved CO₂ in the culture broth were conducted both in situ with a probe as well as using exhaust gas analysis and both the methods of quantification showed good qualitative congruence.     

Influence of agitation and aeration on growth and antibiotic production by <Emphasis Type="Italic">Xenorhabdus nematophila</Emphasis>

The effect of agitation and aeration on the growth and antibiotic production by Xenorhabdus nematophila YL001 grown in batch cultures were investigated. Efficiency of aeration and agitation was evaluated through the oxygen mass transfer coefficient (K _L a). With increase in K _L a, the biomass and antibiotic activity increased. Activity units of antibiotic and dry cell weight were increased to 232 U ml⁻¹ and 19.58 g l⁻¹, respectively, productivity in cell and antibiotic was up more than 30% when K _L a increased from 115.9 h⁻¹ to 185.7 h⁻¹. During the exponential growth phase, DO concentration was zero, the oxygen supply was not sufficient. So, based on process analysis, a three-stage oxygen supply control strategy was used to improved the DO concentration above 30% by controlling the agitation speed and aeration rate. The dry cell weight and activity units of antibiotic were further increased to 24.22 g l⁻¹ and 249 U ml⁻¹, and were improved by 24.0% and 7.0%, compared with fermentation at a constant agitation speed and a constant aeration rate (300 rev min⁻¹, 2.5 l min⁻¹).     

Interactions of cell morphology and transport processes in the lovastatin fermentation

The cholesterol lowering drug, Lovastatin (Mevacor), acts as an inhibitor of HMGCoA reductase, and is produced from an Aspergillus terreus fermentation.Pilot scale studies were carried out in 800 liter fermenters to determine the effects of cell morphology on the oxygen transport properties of this fermentation. Specifically, parallel fermentations giving (i) filamentous mycelial cells, and (ii) discrete mycelial pellets, were quantitatively characterized in terms of broth viscosity, availability of dissolved oxygen, oxygen uptake rates and the oxygen transfer coefficient under identical operating conditions.The growth phase of the fermentation, was operated using a cascade control strategy which automatically changed the agitation speed with the goal of maintaining dissolved oxygen at 50% saturation. Subsequently stepwise changes were made in agitation speed and aeration rate to evaluate the response of the mass transfer parameters (DO, OUR, and k _L a). The results of these experiments indicate considerable potential advantages to the pellet morphology from the standpoint of oxygen transport processes.List of Symbols DO % sat. Dissolved oxygen concentration - k _L a h^–1 Gas-liquid mass transfer coefficient - OUR mmol/dm³h Oxygen uptake rate - P/V KW/m³ Agitator power per unit volume - V _s m/s Superficial air velocity - _app cP Apparent viscosity     

Oxygen-absorption rate-controlled feeding of substrate into aerobic microbial cultures

A system of automatic control of substrate inflow into an aerated culture of microorganisms which depend on oxygen-absorption rate (OAR) has been devised and tested. As the control variable, dissolved oxygen concentration (DOC), which shows the equilibrium between OAR and oxygen-uptake rate in the microbial culture, was chosen. If the equilibrium is disturbed by changes in OAR, then the oxygen-uptake rate is changed by substrate limitation. The DOC is measured by means of a Clark-type polarographic electrode, and the signal is used to actuate the substrate inflow valve or pump. The oxygen-uptake rate changes of microorganisms, after the addition or exhaustion of substrate in the medium, are so rapid that they can be used for this type of control. Fundamental equations were derived and graphical solutions for the control system parameters were suggested for the steady-state relations between DOC, oxygen-uptake rate, specific growth rate, substrate concentration, K_La, and concentration of microorganisms. The system is stable in the entire range of the uptake rates up to nearly the maximum attainable in unlimited substrate conditions, and can be operated in batch feed or continuous flow modifications. It was experimentally tested with the yeast Saccharomyces cerevisiae. The complete utilization of aeration-system capacity of the fermentor was achieved with high yeast yield and no alcohol formation. The quality of the product was excellent.     

The effect of a redox agent,methylene blue,on the survival ofPorphyromonas gingivalis in vitro

Methylene blue, at a concentration of 1.0 mg/ml, was able to raise the redox potential (E_h) of pre-reduced culture medium from –288 mV to –154 mV and to poise the medium at an E_h of –171 mV during 48-h incubation in an anaerobic atmosphere. Addition of the dye to suspensions of the anaerobic periodontopathogen,Porphyromonas gingivalis, to give a final concentration of 1.0 mg/ml raised their E_h to –125 mV. During a 24-h period of anaerobic incubation, the dye maintained the E_h at a level (–150 mV) that was more than 200 mV higher than control, dye-free suspensions, and this was accompanied by at least a 6-log reduction in the viable count. The bactericidal effect of the methylene blue could be counteracted by the reducing agent dithiothreitol at a concentration of 2.0 mg/ml, which lowered the E_h to a level (–333 mV) similar to that of controls. These results have demonstrated that the presence of 1.0 mg/ml methylene blue, in its oxidized form, in an environment is inimical to the survival ofP. gingivalis and that this is related, directly or indirectly, to its ability to raise the E_h of the environment. Topical application of methylene blue, or other redox agents, may be an effective means of eliminating this organism from the periodontal pockets of patients with chronic periodontitis.     

Factors Influencing the Production of a Novel Compound, 7,10-Dihydroxy-8(<Emphasis Type="Italic">E</Emphasis>)-octadecenoic Acid,by <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> PR3 (NRRL B-18602) in Batch Cultures

Pseudomonas aeruginosa PR3 (NRRL B-18602) converts oleic acid to a novel compound, 7,10-dihydroxy-8(E)-octadecenoic acid (DOD). Parameters that included medium volume, cell growth time, gyration speed, pH, substrate concentration, and dissolved oxygen concentration were evaluated for a scale-up production of DOD in batch cultures using Fernbach flasks and a bench-top bioreactor. Maximum production of about 2 g DOD (38% yield) was attained in Fernbach flasks containing 500 ml medium when cells were grown at 28°C and 300 rpm for 16–20 h and the culture was adjusted to pH 7 prior to substrate addition. Increases of medium volume and substrate concentration failed to enhance yield. When batch cultures were initially conducted in a reactor, excessive foaming occurred that made the bioconversion process inoperable. This was overcome by a new aeration mechanism that provided adequate dissolved oxygen to the fermentation culture. Under the optimal conditions of 650 rpm, 28°C, and 40–60% dissolved oxygen concentration, DOD production reached about 40 g (40% yield) in 4.5 L culture medium using a 7-L reactor vessel. This is the first report on a successful scale-up production of DOD. Received: 26 September 2002 / Accepted: 24 October 2002     

Studies on the production of lipase from recombinant Staphylococcus carnosus

Summary Production of lipase from recombinant Staphylococcus carnosus pLipPS2 was studied in standard stirred tank bioreactors. Only low lipase activity was obtained under conventional operating conditions, i.e., moderate to high stirring speeds and aeration rates for keeping the dissolved oxygen concentration at high levels. Additional targetted experiments indicated that the reason for the observed low lipase activity is lipase inactivation due to surface forces and shear stress at the gas/liquid interface. Therefore, a cultivation strategy is proposed that minimizes gas/liquid interfacial area and maximizes the driving concentration for O₂ mass transfer by controlling the dissolved oxygen to low values by gentle stirring and low aeration rates. Thus, high lipase activities can be obtained even in larger scale standard stirred tank bioreactors. Offprint requests to: W.-D. Deckwer     

Influence of hyperbaric oxygen tension on growth parameters of Candida tropicalis and Rhodococcus erythropolis

Summary Oxygen-limited growth was avoided by means of oxygen-enriched aeration in aerobic fermentation processes. Studies were carried out with Candida tropicalis (Cast.) Berkhout and Rhodococcus erythropolis (DSM 43215). The effect of hyperbaric dissolved oxygen tension on growth parameters was examined by varying the dissolved oxygen concentration and the carbon source (glucose, ethanol, and n-alkanes). Up to an oxygen concentration of 40 mg/l in the culture suspension no impairment of the economic coefficients and no promotion of cell lysis was found. It was observed that raised oxygen concentrations in the aeration gas led to enhanced specific growth rates. At cell concentrations above 20 g/l dry weight an uncoupling of carbon source dissimilation and biomass production was observed even at non-limiting oxygen concentrations.     

Correlation of anaerobic biodegradability and the electrochemical characteristic of azo dyes

Some experiments were conducted to study some electrochemical factors affecting the bacterial reduction (cleavage) of azo dyes, knowledge of which will be useful in the wastewater treatments of azo dyes. A common mixed culture was used as a test organism and the reductions of Acid Yellow 4, 11, 17 and Acid Yellow BIS were studied. It was found that the azo dyes were reduced at different rates, which could be correlated with the reduction potential of the azo compounds in cyclic voltammetric experiments. Acid Yellow BIS (E _r − 616.75 mV) was reduced at the highest rate of 0.0284 mol g dry cell weight⁻¹ h⁻¹, Acid Yellow 11 (E _r − 593.25 mV) at 0.0245 mol g dry cell weight⁻¹ h⁻¹ and Acid Yellow 4 (E _r − 513 mV) at 0.0178 mol g dry cell weight⁻¹ h⁻¹. At the same time, the decolourization rate of Acid Yellow 17 (E _r − 627.5 mV) was 0.0238 mol g dry cell weight⁻¹ h⁻¹, which was affected by the nature of chlorine substituent. Reduction of these azo dyes did not occur under aeration conditions. These studies with a common mixed culture indicate that the reduction of azo dyes may be influenced by the chemical nature of the azo compound. The reduction potential is a preliminary tool to predict the decolourization capacity of oxidative and reductive biocatalysts.     

Oxygen transfer to mixed cultures in tower systems

A modified dynamic method is introduced to determine the oxygen transfer coefficient, K_L a, in aerobic fermentation systems which are not mechanically agitated. The dissolved oxygen concentration is measured continuously following a step down or a step up in aeration rate. The response curve is analyzed to obtain the value of K_La Experiments were carried out at several different air flow rates using mixed culture in concurrent tower fermentors with motionless mixers. The effect of sieve trays and Koch motionless mixers on oxygen transfer was investigated using a 3 in. diameter column. The values of K_L aobtained at the bottom of each column were found to be higher than those obtained at the top. Comparison of the results showed that the values ofK_L a were higher when the Koch mixers were used than when the sieve trays were employed. The oxygen uptake rate by the organisms rX, is also calculated by using the K_L a values obtained. They compare favorably withthe experimentally measured values.     

Nrf2‐Mediated Resistance to Oxidant‐Induced Redox Disruption in Embryos

Events that control developmental changes occur during specific windows of gestation and if disrupted, can lead to dysmorphogenesis or embryolethality. One largely understudied aspect of developmental control is redox regulation, where the untimely disruption of intracellular redox potentials (E_h) may alter development, suggesting that tight control of developmental‐stage–specific redox states is necessary to support normal development. In this study, mouse gestational day 8.5 embryos in whole embryo culture were treated with 10 μM dithiole‐3‐thione (D3T), an inducer of nuclear factor (erythroid‐derived 2)‐like 2 (Nrf2). After 14 hr, D3T‐treated and ‐untreated conceptuses were challenged with 200 μM hydrogen peroxide (H₂O₂) to induce oxidant‐induced change to intracellular E_hs. Redox potentials of glutathione (GSH), thioredoxin‐1 (Trx1), and mitochondrial thioredoxin‐2 (Trx2) were then measured over a 2‐hr rebounding period following H₂O₂ treatment. D3T treatment increased embryonic expression of known Nrf2‐regulated genes, including those responsible for redox regulation of major intracellular redox couples. Exposure to H₂O₂ without prior D3T treatment produced significant oxidation of GSH, Trx1, and Trx2, based on E_h values, where GSH and Trx2 E_h recovered, reaching to pre‐H₂O₂ E_h ranges, but Trx1 E_h remained oxidized. Following H₂O₂ addition in culture to embryos that received D3T pretreatments, GSH, Trx1, and Trx2 were insulated from significant oxidation. These data show that Nrf2 activation may serve as a means to protect the embryo from chemically induced oxidative stress through the preservation of intracellular redox states during development, allowing normal morphogenesis to ensue.     

Production of microalgae from olive mill wastewater

With olive mill wastewater (alpechin) used as a nutrient medium, the influence of the aeration level and the composition of the culture medium were analysed in relation to the concentration of alpechin and KNO₃ added in a batch culture of the microalgae Chlorella pyrenoidosa and Scenedesmus obliquus. The pH and temperature of the culture were previously fixed at 6.5 and 30°C. As kinetic parameters, the maximum specific growth rate (μ_m) and the biomass productivity (P_max) were determined. The biomass composition obtained was evaluated for chlorophyll and crude protein content as well as fatty-acid composition corresponding to the lipid fraction. To achieve a balanced biomass composition in terms of proteins and lipids, the most suitable conditions included an alpechin concentration of 10%, without the addition of nitrates and with an aeration level of 1 v/v min. Under these conditions, the μ_m values reached with both microalgae were around 0.03h⁻¹.     

Vergleich von Messungen des kLa-Wertes nach der stationären und der dynamischen Methode bei der Fermentation von L-Lysin und Turimycin

The calculation and scale-up of fermentation processes need k_La as one of the most important engineering data. There are two methods to determine k_La depending on power input, aeration rate and the properties of the fermentation broth: static with a balance between air supply and exit, dynamic gassing out with following the changes of dissolved oxygen concentration during periods of air off and a following air on. Within early intervals of fermentation time the data from both methods agree well, while for later time intervals the dynamic method always gives much lower values for k_La than static. The only explanations for this phenomenon are quick changes in the oxygen metabolism or an enzymatic storage of oxygen. For both gassing out and saturation period it is possible to calculate the same absolute amounts of this additional oxygen.     

Effect of dissolved oxygen concentration and impeller tip speed on itaconic acid production by Aspergillus terreus

Summary Effect of aeration rate and impeller tip speed on mycelium growth and itaconic acid production was investigated in a batch culture of Aspergillus terreus IFO-6365. When impeller tip speed was 94.2 cm/sec at a fixed aeration rate of 0.5 vvm, itaconic acid concentration was 3.6 and 1.6 times higher than those in the impeller tip speed of 62.8 and 125.7 cm/sec, respectively. When an oxygen-enriched air was supplied at a fixed impeller tip speed of 94.2 cm/sec and dissolved oxygen concentration was maintained in the 20–60 % range, both itaconic acid concentration and mycelium growth were not affected by the dissolved oxygen concentration.     

Effects of oxygen volumetric mass transfer coefficient on transglutaminase production by Bacillus circulans BL32

The effects of oxygenation in cultures of Bacillus circulans BL32 on transglutaminase (TGase) production and cell sporulation were studied by varying the agitation speed and the volume of aeration. Kinetics of cultivations has been studied in batch systems using a 2 L bioreactor, and the efficiency of agitation and aeration was evaluated through the oxygen volumetric mass transfer coefficient (k_La). It was adopted a two-stage aeration rate control strategy: first stage to induce biomass formation, followed by a second stage, in which cell sporulation was stimulated. A correlation of TGase production, spores formation, and oxygen concentration was established. Under the best conditions (500 rpm; 2 vvm air flow, followed by no air supply during stationary phase; k_La of 33.7 h⁻¹), TGase production reached a volumetric production of 589 U/L after 50 h of cultivation and the enzyme yield was 906 U/g cells. These values are 61% higher than that obtained in shaker cultures and TGase productivity increased 82%, when k_La varied from 4.4 to 33.7 h⁻¹. The maximal cell concentration increased four times in relation to shaker cultures and the cultivation time for the highest TGase activity was reduced from 192 h to just 50 h. These results show the importance of bioprocess design for the production of microbial TGase, especially concerning the oxygen supply of cultures and the induction of cell sporulation.     

Bacteriology of manganese nodules: III. Reduction of MnO(2) by two strains of nodule bacteria

MnO₂ reduction by aerobic growing cultures of Bacillus 29 and coccus 32, isolated from ferromanganese nodules, was assessed for 7 days. A 1-day lag was observed before the onset of MnO₂ reduction by either culture. Addition of HgCl₂ to a final concentration of about 10^-3 M caused a rapid cessation of MnO₂ reduction by the growing cultures. Neither culture reduced MnO₂ when grown under continued anaerobiosis from the start of an experiment. However, if conditions were made anaerobic after MnO₂ reduction was initiated, reduction continued at a rate only slightly lower than that under aerobic conditions. Resting-cell cultures reduced MnO₂ equally well aerobically and anaerobically, provided that ferricyanide was present to serve as electron carrier. These findings showed that oxygen is needed for culture adaptation to MnO₂ reduction, and that oxygen does not interfere with microbial MnO₂ reduction itself. Both cultures caused sharp drops in the pH of the medium during MnO₂ reduction: with coccus 32, during the entire incubation time; with Bacillus 29, for the first 3 days. The E_h of the medium fluctuated with either culture and never fell below 469 mv with Bacillus 29 and below 394 mv with coccus 32. The rates of glucose consumption and Mn²⁺ release by Bacillus 29 and coccus 32 were fairly constant, but the rates of lactate and pyruvate production were not. Although acid production undoubtedly helped in the reduction of pyrolusite (MnO₂) by the bacteria, it did not appear to be important in the reduction of manganese oxide in ferromanganese nodules, as shown by the results with a nodule enrichment.     

Bacteriology of Manganese Nodules: III. Reduction of MnO2 by Two Strains of Nodule Bacteria1

MnO₂ reduction by aerobic growing cultures of Bacillus 29 and coccus 32, isolated from ferromanganese nodules, was assessed for 7 days. A 1-day lag was observed before the onset of MnO₂ reduction by either culture. Addition of HgCl₂ to a final concentration of about 10^-3 M caused a rapid cessation of MnO₂ reduction by the growing cultures. Neither culture reduced MnO₂ when grown under continued anaerobiosis from the start of an experiment. However, if conditions were made anaerobic after MnO₂ reduction was initiated, reduction continued at a rate only slightly lower than that under aerobic conditions. Resting-cell cultures reduced MnO₂ equally well aerobically and anaerobically, provided that ferricyanide was present to serve as electron carrier. These findings showed that oxygen is needed for culture adaptation to MnO₂ reduction, and that oxygen does not interfere with microbial MnO₂ reduction itself. Both cultures caused sharp drops in the pH of the medium during MnO₂ reduction: with coccus 32, during the entire incubation time; with Bacillus 29, for the first 3 days. The E_h of the medium fluctuated with either culture and never fell below 469 mv with Bacillus 29 and below 394 mv with coccus 32. The rates of glucose consumption and Mn²⁺ release by Bacillus 29 and coccus 32 were fairly constant, but the rates of lactate and pyruvate production were not. Although acid production undoubtedly helped in the reduction of pyrolusite (MnO₂) by the bacteria, it did not appear to be important in the reduction of manganese oxide in ferromanganese nodules, as shown by the results with a nodule enrichment.     

Pullulan fermentation in a reciprocating plate bioreactor

Reciprocating plate bioreactors are particularly well suited for conducting fermentations which give rise to highly viscous broth. To evaluate their performance for polysaccharide fermentations, a series of pullulan fermentations were performed with a particular emphasis placed on the influence of aeration on both the quantity and quality of the product. Two experiments were conducted at constant aeration rates and two others with constant dissolved oxygen concentrations. For the latter two experiments, the dissolved oxygen concentration was controlled by manipulating either the aeration flow rate or the reciprocating frequency of the perforated plates.It was found that, in general, a higher dissolved oxygen concentration leads to a higher productivity but the quality of the product, expressed in terms of the viscosity of the fermentation broth, was nevertheless reduced. It appears that the optimum yield, in terms of both quantity and quality, would be achieved at an intermediate dissolved oxygen concentration.List of Symbols DO mg/l Dissolved oxygen concentration - f Hz Agitation frequency - K _L a s^–1 Volumetric mass transfer coefficient - P g/l Pullulan concentration - Q vvm, l/min Volumetric gas flow rate - X g/l Biomass concentration Greek Letters s^–1 Shear rate - Pa.s Apparent viscosity We wish to acknowledge the financial contribution of l'Association des femmes diplômées des Universités (AFDU) and the National Science and Engineering Research Council of Canada (NSERC).