Effect of the aeration and agitation parameters on the oxytetracycline biosynthesis process under microkinetic conditions

The effect of the aeration levels in flasks on the rate of oxytetracycline biosynthesis and other kinetic characteristics was studied. It was shown that changes in the medium volume in flasks, dilution of the fermentation broth with water or its filtrate and the use of oxygen for aeration had a significant effect on the characteristics studied. Special experiments with low concentrations of the biomass were performed for investigation of the effect of dissolved carbon dioxide on the kinetics of the process.     

The effect of aeration and agitation on tetracycline biosynthesis

The results of the study on relation between tetracycline biosynthesis and the specific power input for agitation in pilot plant apparatus was studied. No correlation was observed between the levels of tetracycline biosynthesis and changes in the specific power input within a range of 0.6 to 2.3 kW/m3 at the expense of changes in the mixer diameter and the agitation rate, when the aeration rate was constant. It was shown that the aeration conditions were most significant for tetracycline biosynthesis. The study provided determination of the optimal aeration conditions for biosynthesis of tetracycline.     

Effect of the aeration and agitation states on tetracycline biosynthesis in semiproduction-capacity apparatus]

The results of the experiments on determination of the effect of aeration and agitation conditions on biosynthesis of tetracycline in the apparatus of semi-production capacity are discussed. It was shown that the antibiotic production level was not connected with the rate of oxygen solution expressed in the sulphite numbers, i.e. this parameter cannot be used as a scaling-up criterion. Accumulation of the antibiotic in the fermentation broth depended on the volume of the air supplied for aeration. It was determined that the level of CO2 dissolved in the fermentation broth did not reach the values having an inhibitory effect on the biosynthetic process.     

Optimization of agitation and aeration conditions for maximum virginiamycin production

To maximize the productivity of virginiamycin, which is a commercially important antibiotic as an animal feed additive, an empirical approach was employed in the batch culture of Streptomyces virginiae. Here, the effects of dissolved oxygen (DO) concentration and agitation speed on the maximum cell concentration at the production phase, as well as on the productivity of virginiamycin, were investigated. To maintain the DO concentration in the fermentor at a certain level, either the agitation speed or the inlet oxygen concentration of the supply gas was manipulated. It was found that increasing the agitation speed had a positive effect on the antibiotic productivity independent of the DO concentration. The optimum DO concentration, agitation speed and addition of an autoregulator, virginiae butanolide C (VB-C), were determined to maximize virginiamycin productivity. The optimal strategy was to start the cultivation at 450 rpm and to continue until the DO concentration reached 80%. After reaching 80%, the DO concentration was maintained at this level by changing the agitation speed, up to a maximum of 800 rpm. The addition of an optimal amount of the autoregulator VB-C in an experiment resulted in the maximal production of virginiamycin M (399 mg/l), which was about 1.8-fold those obtained previously. Received: 13 July 1998 / Received revision: 19 August 1998 / Accepted: 13 September 1998     

Effect of aeration and agitation on the biosynthetic activity of diffusely growingAspergillus niger

A considerable lowering of aeration demands occurs during diffuse growth of citric acid-producingAspergillus niger in a submerged cultivation. However, the diffuse culture poses stricter demands on the type of aeration and agitation. The impeller frequency affects considerably the morphology of the producer fungus and the accumulation of citric acid. The effect of impeller frequency on the distribution of air in the medium and on the amount of air fed into the diffuse culture is less important.     

Distribution of oleandomycin between the native broth and butylacetate depending on the biosynthesis conditions]

Distribution of the active substance contained in the fermentation broth of Act. antibioticus between the acqueous phase and butylacetate depended on the fermentation conditions and the procedure for the fermentation broth treatment before filtration. Increase in pH values during the fermentation process resulted in lower antibiotic distribution coefficients which may be explained by the presence of oleandomycin-X, a biologically active substance in the fermentation broth filtrates. This substance differed from oleandomycin and did not pass into butylacetate from the acqueous alkaline solution. For transference of oleandomycin-X into oleandomycin exposition of the fermentation broth filtrate at pH 5.0--5.5 is required.     

Effect of aeration and agitation on yeast inulinase production: a biocalorimetric investigation

Bioprocess and Biosystems Engineering - Air flow rate and agitation speed for inulinase production by Kluyveromyces marxianus were optimized based on metabolic heat release profiles. Shear stress...     

Optimisation of agitation and aeration in fermenters

The problem of optimising agitation and aeration in a given fermenter is addressed. The objective function is total electric power consumed for agitation, compression and refrigeration. The major constraint considered is to ensure that the dissolved oxygen concentration is above the critical value. It is shown that it is possible to analytically calculate the optimal pair (air flowrate, stirrer speed) and that, at least for the industrial antibiotics fermentation used as case-study, the optimum lies within a window for satisfactory operation, limited by other possible constraints to the problem. Savings achievable by optimal operation as compared with current industrial procedure were found to be around 10% at pilot plant scale (0.26 m³) and 20% at full scale (85 m³).List of Symbols A fermenter cross sectional area (m²) - C dissolved oxygen concentration (mole m^–3) - C ^* DO concentration in equilibrium with the gas (mole m^–3) - C _crit critical DO concentration (mole m^–3) - C _p specific heat of air at constant pressure (J kg^–1 K^–1) - C _sp dissolved oxygen set point (mole m^–3) - C _v specific heat of air at constant volume (J kg^–1 K^–1) - D agitator diameter (m) - f pressure correction of air flow-rate - (Fl _g)_F aeration number at flooding - (Fr _g)_F froude number at flooding - k coefficient in expression for mass transfer coefficient - K _La volumetric oxygen transfer coefficient (s^–1) - m power exponent in expression for mass transfer coefficient - n gas flow rate exponent in expression for mass transfer coefficient - n ^* number of impellers - N rotation speed (s^–1) - N _F rotation speed at flooding (s^–1) - N _p unaerated power number - N _pg aerated power number - OUR Oxygen Uptake Rate (mole m^–3 s^–1) - p ₀ atmospheric pressure (N m^–2) - p ₁ compressor exit pressure (N m^–2) - p ₂ pressure at the bottom of the fermenter (N m^–2) - p ₃ pressure at the top of the fermenter (N m^–2) - P _c compression power (W) - P _d power added by expansion (W) - P _ev power removed by evaporation (W) - P _g agitation power (W) - P _m power added by metabolism (W) - P _r power removed by refrigeration (W) - P _t total power (W) - Q air flow-rate at atmospheric conditions (m³ s^–1) - Q _f air flow-rate at average fermenter conditions (m³ s^–1) - s ₀ absolute humidity at atmospheric conditions - s ₃ absolute humidity at fermenter exit - T tank diameter (m) - V liquid volume (m³) - v _s gas superficial velocity (m s^–1) - _i parameter defined in the text - safety margin for dissolved oxygen (mole m^–3) - ratio of specific heats of air - _g agitation efficiency - _c compression efficiency - _r refrigeration efficiency - liquid density (kg m^–3) - _g air density (kg m^–3) - latent heat of vaporisation of water (J kg^–1) The authors are grateful to Elsa Silva, Carlos Lopes, Carlos Aguiar, Fernando Mendes, and Alexandre Cardoso, who helped with parts of this work, and to CIPAN for permission to publish these data.     

Effect of pH,agitation and aeration on hyaluronic acid production byStreptococcus zooepidemicus

Summary The optimum pH for both the rate of production and yield of hyaluronic acid (HA) byStreptococcus zooepidemicus from glucose medium was 6.7±0.2 under anaerobic conditions. High agitation rates (600 rpm) gave superior results compared to 300 rpm. Aeration of the culture (0.3 VVM) improved the HA yield, but not the rate of production and lead to some acetate and CO₂ being formed, in addition to lactate and HA.     

Effect of agitation and aeration on the citric acid production by Yarrowia lipolytica grown on glycerol

The effects of agitation rates from 400 to 900 rpm and aeration rates ranging from 0.18 to 0.6 vvm on biomass and citric acid production on glycerol media by acetate-negative mutants of Yarrowia lipolytica, Wratislavia 1.31 and Wratislavia AWG7, in batch culture were studied. The agitation rates of 800 and 900 rpm (at a constant aeration rate of 0.36 vvm) and aeration rates within the range of 0.24-0.48 vvm (at a constant agitation rate of 800 rpm), which generated dissolved oxygen concentration (DO) higher than 40%, were found the best for citric acid biosynthesis from glycerol. An increase in agitation rate (higher than 800 rpm) and aeration rate (higher than 0.36 vvm) had no impact on DO and citric acid production. The highest citric acid concentration (92.8 g/L) and yield (0.63 g/g) were obtained with Wratislavia 1.31 strain at 0.24 vvm. The highest volumetric citric acid production rate (1.15 g/Lh) and specific citric acid production rate (0.071 g/gh) were reached at 0.48 vvm.     

Effect of aeration and redox potential on the biosynthesis of the antibiotic imbricin]

The relationship between imbricin biosynthesis by Streptomyces imbricatus and the medium aeration and redox potential (Eh) was studied. The influence of the oxygen dissolution velocity within the ranges of 2.9 to 0.5 g O2/l.h was investigated and it was shown that the highest yield of the antibiotic was provided by the maximum velocity. At the background of the intensive aeration (2.9 g O2/l.h) decreasing of Eh by reducing agents such as ascorbic acid, L-thyrosin or K4Fe(CN)6 stimulated the biosynthesis whereas at the lower velocities the process proved to be inhibited. Under conditions of insufficient aeration the biosynthesis stimulation could be provided by increasing the medium Eh by acidifying agents such as K2Cr2O7, K3Fe(CN)6 or KMnO4. It was concluded that intensive synthesis of imbricin required not only efficient aeration but also definite levels of the medium redox potential.     

Effect of the aeration conditions on the biosynthesis of oxytetracycline and the formation of organic acids by a culture of Actinomyces rimosus]

The effect of the aeration conditions on oxytetracycline biosynthesis and production of organic acids by Act. rimosus was studied. Intensive biosynthesis of oxytetracycline in shaken flasks with concentrated complex media was observed at the rate of oxygen dissolution in the liquid ranging from 14 to 25 mg/1/min. Lower rates of the oxygen dissolution up to 7 mg/1/min resulted in decreased rates of the culture growth and the medium component consumption, decreased antibiotic levels, production of significant amounts of pyruvic and acetic acids.     

Effect of aeration and agitation on the production of mycelial biomass and exopolysaccharides in an enthomopathogenic fungus Paecilomyces sinclairii

AIMS: The objective of the present study was to investigate the influence of aeration rate and agitation intensity on the production of mycelial biomass and exopolysaccharide (EPS) in Paecilomyces sinclairii. METHODS AND RESULTS: The P. sinclairii was cultivated under various aeration and agitation conditions in a 5 l stirred-tank bioreactor. The highest mycelial biomass (30.5 g l-1) and EPS production (11.5 g l-1) were obtained at a high aeration rate (3.5 v.v.m.) and at a high agitation speed (250 rev min-1). The apparent viscosities (6000-8000 cP) of fermentation broth increased rapidly towards the end of fermentations at high aeration and agitation conditions. CONCLUSIONS: The high level of dissolved oxygen achieved at a high aeration rate (3.5 v.v.m.) associated with higher hyphal density eventually resulted in enhanced EPS production. Agitation intensity was also proved to be a critical factor influencing on both the mycelial biomass and EPS production: high agitation speeds up to 250 rev min-1 were preferred to the yields of biomass and EPS production. SIGNIFICANCE AND IMPACT OF THE STUDY: The critical effects of aeration and agitation in the culture process of P. sinclairii were found, which is widely applicable to other kinds of basidiomycetes or ascomycetes in their submerged culture processes.     

Effect of agitation rate and impeller design on oxygen transfer coefficients in small bioreactors using surface aeration

The effects of agitation rate and impeller type on the combined oxygen mass-transfer coefficient (kL a) in four different benchtop bioreactors have been examined. Surface oxygenation of a cell culture medium supplemented with fetal bovine serum and distilled deionized water has been studied by passing air through the bioreactor headspace at approximately one headspace volume per minute. A new ribbon-type impeller design using strips of Teflon has been shown to be superior to conventional impeller designs for oxygen transfer.