Aeration conditions in the process of tetracycline biosynthesis. The role of organic acids]

The effect of the aeration conditions on the content of volatile acids in the fermentation broth was studied. It was shown that deterioration of the aeration conditions during the process of biosynthesis in both flasks and 750 1 fermentors resulted in decreased levels of the antibiotic accumulation and was accompanied by a simultaneous increase in the concentration of the volatile acids in the culture fluid. Under unfavourable aeration conditions the volatile acids present in the fermentation broth in higher concentrations than under the optimal conditions had no effect. It was shown that the volatile acid concentration may be used as a parameter for the control of the aeration conditions and as an index of normal biosynthetic process.     

Enhancement of in vitro growth of papaya multishoots by aeration

Efficient micropropagation of papaya (Carica papaya L.) has become crucial for multiplication of specific sex types of papaya or transgenic lines resistant to virus infection. In this study, aeration at different intervals with a 0.02 μm filter disc in the closure of culture flasks ensured exchange of gas components. The effect of aeration on development of multibuds to multishoots was investigated. Multibuds grown in culture flasks after one-week without aeration followed by a two-week aeration treatment caused a 41% increase in the number of shoots ≥0.5 cm, 42% increase in leaf expansion, and 17% increase in leaf numbers in comparison with unaerated materials. Ethylene and oxygen concentrations in the culture flasks were measured by gas chromatography and oxygen electrode at weekly intervals during the culture period. Oxygen concentrations were slightly different between aerated and unaerated culture flasks. Ethylene in the unaerated flask reached the highest level (0.11 ppm) 2 weeks after the treatment, while accumulation of ethylene in the aerated flasks was not detected. The multishoots grown for 3 weeks without aeration showed growth retardation on leaves and epinasty on petioles. This revised version was published online in June 2006 with corrections to the Cover Date.     

Influence of Dissolved Oxygen Levels on Production of l-Asparaginase and Prodigiosin by Serratia marcescens

The effect of dissolved oxygen concentrations on the behavior of Serratia marcescens and on yields of asparaginase and prodigiosin produced in shaken cultures and in a 55-liter stainless-steel fermentor was studied. A range of oxygen transfer rates was obtained in 500-ml Erlenmeyer flasks by using internal, stainless-steel baffles and by varying the volume of medium per flask, and in the fermentor by high speed agitation (375 rev/min) or low rates of aeration (1.5 volumes of air per volume of broth per min), or both. Dissolved oxygen levels in the fermentation medium were measured with a membrane-type electrode. Peak yields of asparaginase were obtained in unbaffled flasks (3.0 to 3.8 IU/ml) and in the fermentor (2.7 IU/ml) when the level of dissolved oxygen in the culture medium reached zero. A low rate of oxygen transfer was accomplished by limited aeration. Production of prodigiosin required a supply of dissolved oxygen that was obtainable in baffled flasks with a high rate of oxygen transfer and in the fermentor with a combination of high-speed agitation and low-rate aeration. The fermentation proceeded at a more rapid rate and changes in pH and cell populations were accelerated by maintaining high levels of dissolved oxygen in the growth medium.     

Effects of the oxygen transfer rate on ferrous iron oxidation by Thiobacillus ferrooxidans

Ferrous iron oxidation by Thiobacillus ferrooxidans was studied in shake flasks and a bubble column under different aeration conditions. The maximum biooxidation rate constant was affected by oxygen transfer only at low aeration intensities. At oxygen transfer rates higher than 0.03 mmol O₂ l⁻¹ min⁻¹, the maximum biooxidation rate constant was about 0.050 h⁻¹ in both shake flasks of different size and the bubble column. The oxygen transfer rate could be used as a basis for scaling up bioreactors for ferrous iron biooxidation by T. ferrooxidans.     

Heterologous expression of Vitreoscilla hemoglobin (VHb) and cultivation conditions affect the alkaloid profile of Hyoscyamus muticus hairy roots

Fast-growing hairy root cultures of Hyoscyamus muticus induced by Agrobacterium rhizogenes offer a potential production system for tropane alkaloids. Oxygen deficiency has been shown to limit growth and biomass accumulation of hairy roots, whereas little experimental data is available on the effect of oxygen on alkaloid production. We have investigated the effect of Vitreoscilla hemoglobin (VHb) expression and cultivation conditions on the complete alkaloid profile of H. muticus hairy roots in shake flasks and in a laboratory scale bioreactor. We optimized the growth medium composition and studied the effects of sucrose, ammonium, nitrate, and phosphate on growth and alkaloid production. Maximum biomass accumulation was achieved with the highest and maximum hyoscyamine content with the lowest sucrose concentration. The optimum nitrate concentration for growth was higher for the VHb line than the control. Neither VHb expression nor aeration improved the hyoscyamine content significantly, thus suggesting that hyoscyamine biosynthesis is not limited by oxygen availability. Interestingly, the effect of VHb expression on the alkaloid profile was slightly different from that of aeration. VHb expression did not affect the concentrations of cuscohygrine, which was increased by aeration. Therefore, the effect of VHb is probably not related only to its ability to increase the intracellular effective oxygen concentration.     

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.     

溶氧对Blakeslea trispora分批发酵生产β-胡萝卜素的影响

在摇瓶和5 L发酵罐中研究了溶氧 (DO) 对Blakeslea trispora分批发酵生产β-胡萝卜素的影响,总结了5 L发酵罐中β-胡萝卜素发酵过程中溶氧的变化规律.结果表明,当500 mL摇瓶装液量为50 mL,转速为240 r/min条件下发酵生产β-胡萝卜素产量最大,达到3.416 g/L; 5 L发酵罐中,在搅拌转速为1 000 r/min,通气量为1.5 vvm的条件下,β-胡萝卜素的产量可达到3.712 g/L,略高于摇瓶,这可能是由于5 L发酵罐中的气液传递和混合状况好于摇瓶,促进了产物的合成.     

The effects of aeration and veratryl alcohol on the production of two laccases by the ascomycete Botryosphaeria sp

The ascomycete, Botryosphaeria sp, produced two extracellular constitutive laccases (PPO-I and PPO-II) active toward the substrates: 2, 2(1)-azino-bis(3-ethyl-benzthiazoline-6-sulfonic acid) [ABTS], and 2,6-dimethoxyphenol (DMP), respectively. The production of both laccases increased when the fungal isolate was grown in the presence of veratryl alcohol, and resulted in optimal laccase production (100- and 25- fold, respectively) at 40 mM. The effect of aeration on growth and laccase production was studied in baffled flasks, and showed that aeration of the cultures increased the production of both enzymes 4-5 fold in the presence of veratryl alcohol. Both laccases were susceptible to inhibition by azide, acetate and chloride anions. Veratryl alcohol inhibited the laccase-catalyzed polymerization of DMP. Growing cultures of Botryosphaeria sp. produced an exopolysaccharide of the beta-glucan type whose synthesis was depressed when grown in the presence of veratryl alcohol.     

Changes in alginate molecular mass distributions, broth viscosity and morphology of Azotobacter vinelandii cultured in shake flasks

The effect of different aeration conditions during the culture of Azotobacter vinelandii on the production and molecular mass of alginate was evaluated in shake flasks. In baffled flasks, the bacteria grew faster and produced less alginate (1.5 g/l) than in conventional (unbaffled) flasks (4.5 g/l). The viscosity of the culture broth was also influenced by the type of flask. Higher final viscosities were attained in unbaffled flasks [520 cP (520 mPa s)] as compared to baffled flasks (30 cP). This latter phenomenon was closely related to the changes in the molecular mass distribution. In either cases, the mean molecular mass increased with culture age; however, at the end of the fermentation, the mean molecular mass of the alginate obtained in unbaffled flasks was fivefold higher than that obtained in baffled flasks. As the culture proceeded, the cells of Azotobacter grown in unbaffled flasks increased in diameter, whereas those cultured in baffled flasks decreased in size. Received: 13 December 1996 / Received revision: 10 April 1997 / Accepted: 27 April 1997     

Scaleup of ajmalicine production by plant cell cultures of Catharanthus roseus

The effect of scaleup on he production of ajmalicine by a Catharanthus roseus cell suspension culture in a selected induction medium were studied. In preliminary experiments it was observed that the culture turned brown and the production was inhibited upon transfer from a shake flask to a stirred bioreactor with forced aeration. Two factors were recognized as the potential origin of the differences between shake flask and bioreactor cultures: gas composition and mechanical shear forces. These factors were studied separately.By recirculating a large part of the exhaust gas, a comparable gas regime was obtained in a bioreactor as occurred in a shake flask cultures. This resulted in the absence of browning and a similar pattern of ajmalicine production as observed in shake flasks. The effect of shear forces could not be demonstrated. However, the experiments showed that the culture may be very sensitive to liquid phase concentrations of gaseous compounds. The effects of k(L)a, aeration rate, CO(2) production rate, and influent gas phase CO(2) concentration on the liquid phase CO(2) concentration are discussed. (c) 1993 John Wiley & Sons, Inc.     

Quantitative Aspects of Growth of the Methane Oxidizing Bacterium Methylococcus capsulatus on Methane in Shake Flask and Continuous Chemostat Culture

S ummary : Experiments were directed towards the production of high biomass concentrations in cultures of Methylococcus capsulatus. In shake flasks the effects of ammonium ion, phosphate ion and various trace metals on growth were studied. In the chemostat the effects on growth of methane limitation, oxygen limitation, aeration, dilution rate, pH value and temperature were studied and carbon balances were made in steady state conditions. Growth in the fermenter was stimulated by the use of Amberlite CG–120 ion exchange resin in the medium. The probability that Amberlite removed a growth, inhibitor is discussed.     

深层液体培养法生产沼泽红假单胞菌

根据沼泽红假单胞菌 (Rhodopseudomonaspalustris)在好氧黑暗条件下也可生长的特性 ,采用液体深层培养方法 ,在通气式发酵罐中进行大规模生产。对培养基中的碳源、氮源、生长因子和微量元素进行了优化 ,用正交试验确定了主要培养基成分的添加量和接种量。在 10 0 0mL三角瓶和 2 5L全自动通气式发酵罐上进行了放大试验 ,在适宜工艺条件下培养 2 4h ,菌体浓度可达 6 0亿 /mL。     

CO2 accumulation in bioreactor suspension cultures of Cyclamen persicum Mill. and its effect on cell growth and regeneration of somatic embryos

CO₂ accumulation in different culture systems containing embryogenic cell suspension cultures of cyclamen (Cyclamen persicum Mill.) was analyzed. In bioreactors equipped with a bubble-free or a bubble aeration system, CO₂ mole fractions in the gas phase of more than 10% were determined whereas in Erlenmeyer flasks, CO₂ mole fractions were below 2%. CO₂ accumulation in bioreactors was severely growth inhibiting in comparison to the flasks. By removing CO₂ in the aeration gas of a bubble-free aerated bioreactor, cell growth comparable to that in flasks was achieved. The regeneration ability of cell suspensions after being cultured in bioreactors with CO₂ accumulation was better than those after culture in bioreactors without CO₂ accumulation or in flasks. Received: 16 June 1998 / Revision received: 13 August 1998 / Accepted: 1 December 1998     

Effect of forced aeration on citric acid production by Aspergillus sp. mutants in SSF

Citric acid (CA) is one of the most important products of fermentation in the world. A great variety of agro-industrial residues can be used in solid state fermentation. Aspergillus niger parental strain (CCT 7716) and two strains obtained by mutagenesis (CCT 7717 and CCT 7718) were evaluated in Erlenmeyer flasks and glass columns using citric pulp (CP) as substrate/support, sugarcane molasses and methanol. Best results using glass columns (forced aeration) were found in the fourth day of fermentation: 278.4, 294.9 and 261.1 g CA/kg of dry CP with CCT 7716, CCT 7718 and CCT 7717, respectively. In Erlenmeyer flasks (aeration by diffusion) CA reached 410.7, 446.8 and 492.7 g CA/kg of dry CP with CCT 7716, CCT 7718 and CCT 7717, respectively. The aeration by diffusion improved CA production by the three strains. A data acquisition system specially developed for biotechnological processes analysis was used to perform the respirometric parameters measurement.     

Effect of oxygen supply on the suspension culture of genetically modified tobacco cells.

The effect of oxygen supply on the cultivation of the genetically modified tobacco cells and the formation of a foreign protein, beta-glucuronidase (GUS), was investigated in 250-mL Erlenmeyer flasks, a 5-L stirred tank fermenter, and a 7-L air-lift fermenter. The oxygen supply was varied by using different volumes of medium in the case of the 250-mL Erlenmeyer flask culture or by the different aeration rate in the case of the two types of fermenters tested. Higher oxygen supply stimulated cell growth and increased oxygen consumption rate, the level of phenolics, and GUS productions.     

Determination of CO₂ sensitivity of micro-organisms in shaken bioreactors. I. Novel method based on the resistance of sterile closure

Influence of carbon dioxide on growth and product kinetics of industrially important micro-organisms is essential for the interpretation of a bioprocess. In this research, the CO? effects on productivity and growth rate of micro-organisms have been studied by using a variety of kplug. The applied method is based on a different concentration of CO? in the headspace of ventilation flasks. The presented method is simple, inexpensive and shows similar results compared to large-scale fermentation regarding the evolution of CO? in a batch system. For the investigation of the proposed method, experiments employing Arxula adeninivorans LS3, Corynebacterium glutamicum (DM1730 and ATCC WT13032) and Hansenula polymorpha DSM70277 as model organisms in the ventilation flasks are performed. The fermentations in the RAMOS (respiratory activity monitoring system) device were carried out with a normal aeration rate (1 vvm) and under the same operating conditions as the ventilation flask f1. The modified unsteady-state model was used to predict the operation conditions of a biological system in the ventilation flasks. In the present study, a novel and easy method for the quantification of CO? sensitivity of micro-organisms in shaken bioreactors (called ventilation flask) was achieved.     

Effects of oxygen on recombinant protein production by suspension cultures of Spodoptera frugiperda (Sf-9) insect cells.

Spodoptera frugiperda (Sf-9) insect cells have been grown in serum-free medium in 250-ml spinner flasks. The maximum cell density obtained in these cultures was dependent on the aeration rate of the culture. Similar yields of uninfected cells were obtained when cultures were stirred in spinner flasks at 80 rev min-1 and in a 4-1 stirred-tank bioreactor and the dissolved oxygen in the bioreactor was controlled at 20% of air saturation. Cells were infected with a recombinant baculovirus at different multiplicities of infection: the timing and maximum level of expression of the recombinant protein were dependent on the multiplicity of infection, the cell density at infection, and on the aeration rate of the culture. Oxygen-limited growth resulted in undetectable levels of recombinant protein (< 6 ng recombinant protein 10(-7) cells). Compared with the maximum yields observed in spinner flask cultures, higher levels of recombinant protein were produced when cells were grown and infected in the bioreactor. The level of dissolved oxygen in the bioreactor was controlled at 50% of air saturation.     

A large, efficient and inexpensive bacterial growth chamber

The construction of a 200 liter bacterial growth chamber for a total cost of less than $400 is described. The chamber was designed for growth of aerobic organisms and therefore provides high rates of aeration and mixing. The growth of Escherichia coli K₁₂ in the chamber was similar to growth in small flasks on a rotary shaker. Azotobacter vinelandii OP growth is slower in the growth chamber than in small, shaken flasks. Under the growth conditions described, kilogram quantities of bacterial cells are obtained from a single culture.     

Scaled-up proliferation and regeneration of Nerine in liquid cultures Part I. The induction and maintenance of proliferating meristematic clusters by paclobutrazol in bioreactors

The natural propagation rate of bulb forming Amaryllidaceae including Nerine is low. Conventional micropropagation techniques are labor intensive and therefore expensive. Liquid cultures facilitate: scaling up, automation and cost reduction of micropropagation. Inflorescence-derived explants of Nerine were cultured on 2,4-dichlorophenoxyacetic acid (2,4-d) and 6-benzyladenine (BA) supplemented Murashige & Skoog (MS) medium. Callus-like tissue interspersed with nodular tissue, as well as direct organogenesis developed at the junction between flower pedicel and peduncle. Subculture of nodular tissue to 1-naphthalene acetic acid (NAA), BA and paclobutrazol (PAC) supplemented liquid medium in Erlenmeyer flasks or bubble bioreactors resulted in proliferation of rounded, compact, easily crumbled meristematic clusters. Growth and proliferation in bioreactors were higher than in shaken flasks and were affected differently by the inoculum to medium ratio in the two types of culture vessel. Nerine cultures showed low sensitivity to high aeration rates in bubble bioreactors despite the accumulation of debris. It was therefore possible to increase aeration rates without reducing the proliferation rate or damaging the quality of the meristematic aggregates. The conditions in semi-continuous culture in flasks and bioreactors were more favorable and increased the growth value by 100% and 140%, respectively. The total protein content increased by 180% in flasks and 90% in bioreactors. Although the presence of PAC throughout the culture period decreased growth and proliferation, it was a promotive bioregulator for meristernatic cluster formation. Proembryogenic clusters developed upon the removal of PAC. The use of meristematic clusters for micropropagation in scaled-up liquid cultures is discussed.     

Degradation of naphthalene to salicylic acid by cultures ofPseudomonas denitrificans andAchromobacter sp. from the effluents of petroleum refinery

The microbial degradation of aromatic hydrocarbons from effluents of a petroleum refinery was investigated, with emphasis on the breakdown of naphthalene to salicylic acid. The microorganisms were grown in a synthetic medium with naphthalene as the sole carbon source. The effects of pH, temperature, aeration and naphthalene concentration were studied. The optimum conditions for degradation were found to be: pH 6.0, 28°C, 25 ml medium with 1% naphthalene in 500 ml flasks. Salicylic acid was estimated by colorimetric and chromatographic methods. Maximum of growth was found on the 5th day of cultivation.Pseudomonas denitrificans produced 9.0 μg salicylic acid per ml medium,Achromobacter sp. produced 7.1 μg/ml.