Effect of oxygen supply on biomass and helvolic acid production in submerged fermentation of Cordyceps taii

The entomogenous fungus Cordyceps taii, a traditional Chinese medicinal mushroom, exhibits potent important pharmacological effects and it has great potential for health foods and medicine. In this work, the effects of oxygen supply on production of biomass and bioactive helvolic acid were studied in shake-flask fermentation of C. taii mycelia. The value of initial volumetric oxygen transfer coefficient (K_La) within 10.1–33.8 h⁻¹ affected the cell growth, helvolic acid production and expression levels of biosynthetic genes. The highest cell concentration of 17.2 g/L was obtained at 14.3 h⁻¹ of initial K_La. The highest helvolic acid production was 9.6 mg/L at 10.1 h⁻¹ of initial K_La. The expression levels of three genes encoding hydroxymethylglutaryl-CoA synthase, hydroxymethylglutaryl-CoA reductase and squalene synthase were down-regulated on day 2 and day 8 but up-regulated on day 14 at an initial K_La value of 10.1 h⁻¹ vs. 33.8 h⁻¹, which well corresponded to the helvolic acid biosynthesis in those conditions. The information obtained would be helpful for improving the biomass and helvolic acid production in large-scale fermentation of C. taii.     

Enhancement of anthocyanin production by Perilla frutescens cells in a stirred bioreactor with internal light irradiation

Oxygen supply and light irradiation exhibited significant influence on the production of anthocyanin (red pigments) by suspended cultures of Perilla frutescens cells in a 2.6-l aerated and agitated bioreactor with a six-flat-bladed turbine. When the initial volumetric oxygen transfer coefficient (k_La) value was below 10 h⁻¹ and light was not irradiated, the anthocyanin production was never over 0.6 g/l. By modification of a gas sparger, the oxygen supply capability of the bioreactor was remarkably improved, and 1.65 g/l of anthocyanin was obtained at an enhanced k_La value of 15.4 h⁻¹. Moreover, it was found that anthocyanin accumulation at a 0.2 vvm aeration rate was higher than that at 0.1 or 0.4 vvm in the modified bioreactor, with the other cultivation conditions kept the same. Light irradiation also significantly increased anthocyanin accumulation in the stirred reactor at a low k_La value, i.e. 9.9 h⁻¹. However, a combination of irradiation with a higher oxygen supply reduced the production of anthocyanin in the bioreactor.     

Effect of ventilation on the production of acetaldehyde by Zymomonas mobilis

The production of acetaldehyde, a flavoring agent in food, by Zymomonas mobilis was carried out in batch culture. The volatilization rate constant (k_v) of acetaldehyde and the initial volumetric oxygen transfer coefficient (k_La⁰) in an Erlenmeyer flask with a cotton-plug (cotton-flask) and an aerated-flask with a forced-air system (aerated-flask) were measured. The culture environment in the aerated-flask was found to be very different from that in the cotton-flask. Cell growth in a cotton-flask was strongly inhibited, making practical acetaldehyde production in cotton-flask very difficult. On the other hand, acetaldehyde production in the aerated-flask increased while the fermentation time decreased with increases in the air flow rate. The k_v value of acetaldehyde in a jar fermentor was affected mainly by air flow rate. By considering both the oxygen transfer rate and the ventilation effect on the culture, it was possible to scale-up from the aerated-flask to a jar fermentor. In the jar fermentor, production of acetaldehyde and growth inhibition by acetaldehyde were affected mainly by the k_La⁰ and k_v, values, respectively. The overall production of acetaldehyde in the jar fermentor under the optimum k_La⁰ and k_v conditions was 6.64 g/l (Y_p/s: 0.27), which was about 1.5 times higher than the maximum concentration obtained in the aerated-flask.     

Physiological effects of the addition of n-dodecane as an oxygen vector during steady-state Bacillus licheniformis thermophillic fermentations perturbed by a starvation period or a glucose pulse

The effect of the presence of n-dodecane as a potential oxygen vector during oxygen-limited continuous cultures of a Bacillus strain was studied, under extreme nutrient supply conditions: glucose excess, limitation and starvation. The addition of n-dodecane to the aqueous phase of a mechanically agitated and aerated fermentation increased the k_La by up to 35%. The n-dodecane additions to Bacillus licheniformis cells during starvation (oxygen limitation with concomitant glucose starvation) caused a severe detrimental progressive change in cell physiological state with respect to cytoplasmic membrane polarisation and permeability which was mitigated against by alleviating either the oxygen limitation (by increasing the mean energy dissipation rate or by the addition of n-dodecane as an oxygen vector) or by alleviating the carbon limitation (by resuming the carbon feed or by the addition of a glucose pulse). Further that during periods of excess glucose (glucose pulse) a much higher k_La was required to prevent the onset of anaerobic mixed acid fermentation than could be provided by the addition of n-dodecane alone. n-Dodecane can be used to increase the k_La when added in sufficient quantities to the aqueous phase of a mechanically agitated and aerated bioreactor but the magnitude of this increase is process and vessel geometry specific.     

Cloning, expression and characterization of squalene synthase from Inonotus obliquus

The chaga mushroom Inonotus obliquus has been widely used as a folk medicine in Russia, Poland and most of the Baltic countries. The total triterpene saponins of I. obliquus have significant pharmacological activity. Though the triterpene component has been well characterized in terms of its pharmaceutical activity, there is little information on the genes responsible for the biosynthesis of these compounds in I. obliquus. Squalene synthase represents a potential branching point and the first committed step to diverge the carbon flux from the main isoprenoid pathway towards sterol biosynthesis. In this study, we cloned and characterized squalene synthase from I. obliquus. A 1476-bp full-length cDNA consisting of the entire coding region of squalene synthase (GenBank accession number is KC182754) was cloned by RT-PCR. The DNA sequence showed as much as 76 % similarity with the sequence of Fomitiporia mediterranea squalene synthase, and phylogenetic analysis indicated that it is most closely related to F. mediterranea squalene synthase at both DNA and protein levels. I. obliquus squalene synthase was actively expressed in the yeast Pichia pastoris as a secreted form and purified by gel filtration using Superdex G-75 column. The purified recombinant squalene synthase was able to convert farnesyl diphosphate (FPP) to squalene in an NADPH-dependent reaction. The result of this study could serve as an important step toward the manipulation of triterpenoids biosynthesis in I. obliquus at the level of squalene through engineering better SQS for reintroduction into the mushroom.     

Effects of oxygen volumetric mass transfer coefficient and pH on lipase production by Staphylococcus warneri EX17

The principal objectives of this study were to evaluate the kinetics of lipase production by Staphylococcus warneri EX17 under different oxygen volumetric mass transfer coefficients (k_La) and pH conditions in submerged bioreactors, using glycerol (a biodiesel by-product) as a carbon source. Cultivations were conducted at different k_La (26, 38, 50, and 83 h⁻¹) and pH values (6.0, 7.0, and 8.0). The optimal k_La and pH were 38 h⁻¹ and 7.0, respectively. Under these conditions, the maximal cell production obtained was 8.0 g/L, and the volumetric and specific lipase production reached high levels of activity, approximately 800 U/L and 150 U/g cell, respectively, after 12 h of cultivation. This result was approximately five times higher than that obtained in the shake flask cultures. The relationship between cell growth and lipase production was found to be associated with growth by the Luedeking-Piret model.     

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.     

Biosynthesis of squalene and other triterpenes in Mentha piperita from mevalonate-2-14C

Unlike mono- and sesqui-terpenes, squalene and other triterpenes in peppermint readily incorporate mevalonate-2-¹⁴C label (greater than 30% incorporation of R-mevalonate in 4 hr). The labelled squalene produced turns over rapidly. Squalene derived from mevalonate-2-¹⁴C in incorporation times of 1, 4 and 7 hr was degraded chemically and shown to be equivalently labelled, according to theory, in the isopentenyl pyrophosphate-derived and dimethylallyl pyrophosphate-derived portions of the molecule. This contrasts with earlier studies on the biosynthesis of mono- and sesqui-terpenes in peppermint from ¹⁴C-precursors, in which the isopentenyl pyrophosphate-derived portions of the terpene molecules were found to be preferentially labelled, suggesting the presence of endogenous dimethylallyl pyrophosphate pools. The kinetics of squalene biosynthesis, and the labelling pattern of squalene, suggest that sites of triterpene biosynthesis are readily accessible to exogenous mevalonate and that endogenous dimethylallyl pyrophosphate pools do not participate in triterpene biosynthesis to any appreciable extent. The triterpene biosynthetic sites in peppermint thus appear to differ significantly from the monoterpene and sesquiterpene biosynthetic sites.     

Production and optimization of poly-γ-glutamic acid by Bacillus subtilis BL53 isolated from the Amazonian environment

The aims of this research were to screen and characterize a new microbial source of γ-PGA, to optimize aspects of culture conditions and medium composition using central composite design and response surface methodologies. The influence of bioreactor stirring rates on the production of γ-PGA was also investigated and the oxygen volumetric mass transfer coefficients (k _La) were established. The most productive strain was identified by 16S rDNA analysis as Bacillus subtilis, and its γ-PGA production in rotatory shaker was threefold increased under optimized conditions (37 °C, pH 6.9, and 1.22 mM Zn²⁺), compared to conventional medium. In bioreactor, the γ-PGA production was further increased, reaching 17 g l^?1, 70 % higher than shaker cultures. γ-PGA production showed high dependency on oxygen transfer. At k _La of 210 h^?1, the cultivation time could be reduced to 48 h, about 50 % of the time required for operations at k _La 55 h^?1.     

Optimization of lipase production by <Emphasis Type="Italic">Staphylococcus warneri</Emphasis> EX17 using the polydimethylsiloxanes artificial oxygen carriers

In this research, the combined effects of polydimethylsiloxane (PDMS) and different conditions of oxygen volumetric mass transfer coefficient (k_La) on lipase production by Staphylococcus warneri EX17 were studied and optimized in bioreactor cultures. Raw glycerol from biodiesel synthesis was used as the sole carbon source. Full-factorial central composite design and the response surface methodology were employed for the experimental design and analysis of the results. The optimal polydimethylsiloxane concentration and mass coefficient transfer (k_La) were found to be 13.5% (v/v) and 181 h⁻¹, respectively. Under these conditions, the maximal cell production obtained was 10.0 g/l, and the volumetric lipase activities of approximately 490 U/l, after 6 h of cultivation. These results are in close agreement with the model predictions. Results obtained in this work reveal the positive effects of PDMS on oxygen volumetric mass transfer coefficient (k_La) in the Staphylococcus warneri EX17 cultivation and lipase production.     

Effect of n-dodecane on Crypthecodinium cohnii fermentations and DHA production

The potential use of n-dodecane as an oxygen vector for enhancement of Crypthecodinium cohnii growth and docosahexaenoic acid (DHA) production was studied. The volumetric fraction of oxygen vector influenced the gas–liquid volumetric mass transfer coefficient k _L a positively. The k _L a increased almost linearly with the increase of volumetric fraction of n-dodecane up to 1%. The stirring rate showed a higher influence on the k _L a than the aeration rate. The effects of this hydrocarbon on C. cohnii growth and DHA production were then investigated. A control batch fermentation without n-dodecane addition (CF) and a batch fermentation where n-dodecane 1% (v/v) was added (DF) were carried out simultaneously under the same experimental conditions. It was found that, before 86.7 h of fermentation, the biomass concentration, the specific growth rate, the DHA, and total fatty acids (TFA) production were higher in the CF. After this fermentation time, the biomass concentration, the DHA and TFA production were higher in the DF. The highest DHA content of biomass (6.14%), DHA percentage of TFA (51%), and DHA production volumetric rate r _DHA (9.75 mg l⁻¹ h⁻¹) were obtained at the end of the fermentation with n-dodecane (135.2 h). The dissolved oxygen tension (DOT) was always higher in the DF, indicating a better oxygen transfer due to the oxygen vector presence. However, since the other C. cohnii unsaturated fatty acids percentages did not increase with the oxygen availability increase due to the n-dodecane presence, a desaturase oxygen-dependent mechanism involved in the C. cohnii DHA biosynthesis was not considered to explain the DHA production increase. A selective extraction through the n-dodecane was suggested.     

Effect of molybdenum on secondary metabolic process of glycyrrhizic acid in Glycyrrhiza uralensis Fisch.

A pot experiment was conducted to investigate into effects of molybdenum (Mo) on the secondary metabolic process of glycyrrhizic acid (GA). One-year-old seedlings were grown in pots with washed vermiculite and sand. Hoagland nutrition solution was irrigated with four concentrations: 0, 0.52, 5.2 and 10.4 mg L⁻¹. The accumulations of GA and its biosynthetic precursors (β-amyrin and squalene) and then expression of the key synthase (β-amyrin synthase, β-AS) were studied on 35, 70 and 105 d. In the early stage, that was on the 35 and 70 d, the contents of squalene and GA, and the expression of β-AS gene under 0.52 and 5.2 mg L⁻¹ Mo treatments were significantly higher than that under 0 and 10.4 mg L⁻¹ Mo. There was a contrary result of β-amyrin. However, the content of squalene under 0 mg L⁻¹ Mo was the highest on 105 d. Thus, it suggested an appropriate concentration of Mo could promote the accumulation of GA, by affecting the biosynthetic process of GA at a certain time. Practically, the time and amount of application of Mo on Glycyrrhiza uralensis should be the noted.     

Nocturnal gibberellin biosynthesis is carbon dependent and adjusts leaf expansion rates to variable conditions

Optimal plant growth performance requires that the presence and action of growth signals, such as gibberellins (GAs), are coordinated with the availability of photo-assimilates. Here, we studied the links between GA biosynthesis and carbon availability, and the subsequent effects on growth. We established that carbon availability, light and dark cues, and the circadian clock ensure the timing and magnitude of GA biosynthesis and that disruption of these factors results in reduced GA levels and expression of downstream genes. Carbon-dependent nighttime induction of gibberellin 3-beta-dioxygenase 1 (GA3ox1) was severely hampered when preceded by reduced daytime light availability, leading specifically to reduced bioactive GA₄ levels, and coinciding with a decline in leaf expansion rate during the night. We attributed this decline in leaf expansion mostly to reduced photo-assimilates. However, plants in which GA limitation was alleviated had significantly improved leaf expansion, demonstrating the relevance of GAs in growth control under varying carbon availability. Carbon-dependent expression of upstream GA biosynthesis genes (Kaurene synthase and gibberellin 20 oxidase 1, GA20ox1) was not translated into metabolite changes within this short timeframe. We propose a model in which the extent of nighttime biosynthesis of bioactive GA₄ by GA3ox1 is determined by nighttime consumption of starch reserves, thus providing day-to-day adjustments of GA responses.

GA-sugar matching occurs specifically at night and determines day to day adjustment of GA levels and subsequent growth.     

Mathematical model based estimation of volumetric oxygen transfer coefficient(s) in the production of proteolytic enzymes in Bacillus amyloliquefaciens

Alkaline protease is a class of important hydrolytic enzymes having wide applications in bioprocess industries. Their optimum pH in the alkaline range and stability at higher temperatures make them ideal in detergent and leather processing industries. These enzymes have excellent depilating capacity. The present study aims at process optimization for the production of alkaline protease from Bacillus amyloliquefaciens ATCC 23844. Information on the optimal operating temperature and pH were elicited from specific growth rates and alkaline protease yields. It was also observed that besides pH and temperature, the oxygen transfer rate is another important limiting variable for the production of protease. Volumetric oxygen transfer coefficient (k _L a) was estimated at various impeller speeds and aeration rates. The optimal impeller speed and aeration rates were determined from k _L a and the relative protease yield data. It was understood that the oxygen transfer rate is one of the crucial parameters for the production of proteolytic enzymes by B. amyloliquefaciens.