Effect of flow rate pattern on glucose-6-phosphate dehydrogenase synthesis in fed-batch culture of recombinant Saccharomyces cerevisiae

A strain of genetically modified Saccharomyces cerevisiae (S. cerevisiae) W303 181 was used to improve glucose-6-phosphate dehydrogenase (G6PDH) production in aerobic culture. Fed-batch cultures were carried out in a 5 L fermentor at variable values of the parameter K, namely, 0.2, 0.3, 0.5, 0.7, and 0.8 h(-)(1). The highest G6PDH production (1164 U/L) and specific activity (517 U/g(cell)) were obtained using the following conditions: glucose, 5.0 g/L; adenine, 8 microg/mL; histidine, 8 microg/mL; tryptophan, 8 microg/mL; temperature, 30 degrees C; inoculum, 1.28 g/L; pH, 5.7; agitation, 400 rpm; aeration, 2.2 vvm; and K, 0.2 h(-)(1). The exponential feeding pattern increased cell density (2.14 g/L), enzyme productivity (149.27), and biomass yield (0.18 g(glu)/g(cell)( )(mass)). The level of G6PDH in the genetically modified S. cerevisiae was approximately 4.1-fold higher than that found in a commercial strain.     

Production of carbonyl reductase by Geotrichum candidum in a laboratory scale bioreactor

Fungal fermentation is very complex in nature due to its nonlinear relationship with the time, especially in batch culture. Growth and production of carbonyl reductase by Geotrichum candidum NCIM 980 have been studied in a laboratory scale stirred tank bioreactor at different pH (uncontrolled and controlled), agitation, aeration and dissolved oxygen concentration. The yield of the process has been calculated in terms of glucose consumed. Initial studies showed that fermenter grown cells have more than 15 times higher activity than that of the shake flask grown cells. The medium pH was found to have unspecific but significant influence on the enzyme productivity. However, at controlled pH 5.5 the specific enzyme activity was highest (306U/mg). Higher agitation had detrimental effect on the cell mass production. Dissolved oxygen concentration was maintained by automatic control of the agitation speed at an aeration rate of 0.6 volume per volume per minute (vvm). Optimization of glucose concentration yielded 21g/l cell mass with and 9.77x10(3)U carbonyl reductase activity/g glucose. Adaptation of different strategies for glucose feeding in the fermenter broth was helpful in increasing the process yield. Feeding of glucose at a continuous rate after 3h of cultivation yielded 0.97g cell mass/g glucose corresponding to 29.1g/l cell mass. Volumetric oxygen transfer coefficient (K(L)a) increased with the increasing of agitation rate.     

Development of a stepwise aeration control strategy for efficient docosahexaenoic acid production by Schizochytrium sp.

The effect of aeration on the performance of docosahexaenoic acid (DHA) production by Schizochytrium sp. was investigated in a 1,500-L bioreactor using fed-batch fermentation. Six parameters, including specific growth rate, specific glucose consumption rate, specific lipid accumulation rate, cell yield coefficient, lipid yield coefficient, and DHA yield coefficient, were used to understand the relationship between aeration and the fermentation characteristics. Based on the information obtained from the parameters, a stepwise aeration control strategy was proposed. The aeration rate was controlled at 0.4 volume of air per volume of liquid per minute (vvm) for the first 24 h, then shifted to 0.6 vvm until 96 h, and then switched back to 0.4 vvm until the end of the fermentation. High cell density (71 g/L), high lipid content (35.75 g/L), and high DHA percentage (48.95%) were achieved by using this strategy, and DHA productivity reached 119 mg/L h, which was 11.21% over the best results obtained by constant aeration rate.     

Production of carbonyl reductase by Metschnikowia koreensis

A new strain of the yeast Metschnikowia koreensis was grown in shake flasks and a stirred bioreactor for the production of carbonyl reductase. The optimal conditions in the bioreactor for maximizing the biomass specific activity of the enzyme were found to be: a medium composed of glucose (20 g/L), peptone (5 g/L), yeast extract (5 g/L) and zinc sulfate (0.3g/L); the pH controlled at 7; the temperature controlled at 25 °C; an agitation speed of 500 rpm; and an aeration rate of 0.25 vvm. In the bioreactor, a biomass specific enzyme activity of 115.6 U/gDCW was obtained and the maximum biomass concentration was 15.3 gDCW/L. The biomass specific enzyme activity obtained in the optimized bioreactor culture was 11-fold higher than the best result achieved in shake flasks. The bioreactor culture afforded a 2.7-fold higher biomass concentration than could be attained in shake flasks.     

Optimized production of 2,3-butanediol by a lactate dehydrogenase-deficient mutant of Klebsiella pneumoniae

To obtain high-yield production of 2,3-butanediol (2,3-BD) from glucose, we optimized the culture conditions for a lactate dehydrogenase-deficient mutant (ΔldhA) of Klebsiella pneumoniae using response surface methodology. 2,3-BD production was successfully improved by optimizing pH (5.6), aeration (3.50 vvm) and concentration of corn steep liquor (45.0 mL/L) as a nitrogen source, resulting in a maximum level of 2,3-BD production of 148.8 g/L and productivity of 2.48 g/L/h. 2,3-BD was also obtained with high concentration (76.24 g/L) and productivity (2.31 g/L/h) from the K. pneumoniae mutant strain using sugarcane molasses as a carbon source.     

Fed-batch culture of recombinant Saccharomyces cerevisiae for glucose 6-phosphate dehydrogenase production

We examined glucose 6-phosphate dehydrogenase (G6PD) production by fed-batch cultivation, using a recombinant strain of Saccharomyces cerevisiae W303-181 overexpressing this enzyme. The cultivations were carried out in a 3 L fermenter at pH 5.7, 30 °C, 2.0 vvm aeration, 200 rpm agitation and an inoculum concentration of 1.0 g/L. The volume of the culture medium in the fed-batch process varied from 1.333 to 2.0 L, due to the addition of 15.0 g/L glucose solution during 5 h. Different feeding rates were studied (exponentially increasing and decreasing feeding rates), and the feeding profile was determined by values of the parameter K (time constant), namely: 0.2, 0.5 and 0.8 h⁻¹. The best enzyme production (847 U/L) was obtained with an exponentially increasing feeding rate and K = 0.2 h⁻¹. The results attained also showed that this process is promising for G6PD production.     

Enhanced beta-galactosidase production by high cell-density culture of recombinant Bacillus subtilis with glucose concentration control

Cell concentration, recombinant protein (beta-galactosidase) level, and the specific enzyme expression level were increased from 19 to 184 g/L, 18.3 to 129 U/mL, and 3.2 to 5.7 U/mg protein, respectively, in fed-batch culture of recombinant Bacillus subtilis when glucose concentration was controlled at 1 g/L as compared with those of conventional fed-batch culture. Glucose concentration of the culture broth was monitored by an automatic on-line glucose analyzer and controlled with a moving identification combined with optimal control (MICOC) strategy. When glucose concentrations were controlled at 10, 1, and 0.2 g/L, accumulated propionic acid concentrations and specific enzyme activities were 18.5, 4.4, and 0.6 g/L and 2.9, 5.7, and 7.1 U/mg protein, respectively. The addition of various concentrations of sodium propionate to the growth medium in batch cultures resulted in a drastic decrease in the growth rate with respect to propionate concentration. The propionic acid was shown to be responsible for cell growth inhibition and enzyme activity reduction in fed-batch culture. (c) 1992 John Wiley & Sons, Inc.     

pH shift enhancement of Candida utilis pyruvate decarboxylase production

Pyruvate decarboxylase (PDC) catalyses the synthesis of asymmetric carbinols, e.g., chiral precursors for pharmaceuticals such as ephedrine and pseudoephedrine. The production of PDC by Candida utilis in a minimal medium was improved by manipulating the pH during fermentation in a 5 L bioreactor. At an aeration rate of 0.1 vvm with a stirrer speed of 300 rpm at constant pH 6, a specific PDC activity of 141 U/g dry cell weight (DCW) was achieved (average of two fermentations +/-13%). By allowing the yeast to acidify the growth medium from pH 6 to 2.9, the final specific PDC activity increased by a factor of 2.7 to 385 U/g DCW (average from 4 fermentations +/-16%). The effect of this pH drift on PDC production was confirmed by another experiment with a manual shift of pH from 6 to 3 by addition of 5 M sulfuric acid. The final PDC activity was 392 U/g DCW (average from two fermentations +/-5%). However, experiments with constant pH of 6, 5, 4, or 3 resulted in average specific activities of only 102 to 141 U/g DCW, suggesting that a transitional pH change rather than the absolute pH value was responsible for the increased specific PDC activity.     

Production of chum salmon cystatin from the recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> optimized using response surface methodology

Chum salmon cystatin was overexpressed on Saccharomyces cerevisiae YPH 499. At first, the culture condition for the production of recombinant chum salmon cystatin (RC) by S. cerevisiae YPH 499 was optimized in a shake flask using response surface methodology. Three independent variables; medium pH, inducing time, and the amount of inducing assistant, were analyzed to get the optimal condition for the production of RC. The results were fitted to a second-order polynomial equation, in which the determination coefficient (R ²) was 0.904. The highest RC production in a shake flask, 0.57 U/mL was obtained at 5.7 of medium pH, 6.7 h of inducing time, and 5.6 g/L of inducing assistant. Based on the results of shake flask, the effects of agitation and aeration rates on the production of RC by S. cerevisiae YPH 499 were determined for scaleup in a fermentor. The highest production of RC in a fermentor, 0.56 U/mL was obtained at 350 rpm of agitation rate and 1.0 vvm of aeration rate. RC at 100 μg/g showed the highest inhibitory activity against the autolysis of Alaska pollock surimi based on the analysis of TCA-soluble peptides.     

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.     

Fed-batch fermentation to produce oligonucleotides from Kluyveromyces marxianus grown on whey

Oligonucleotides (ON) extracted from yeasts are used as antiviral agents, immunostimulators, and flavour enhancers. Fed-batch fermentation of cheese whey by Kluyveromyces marxianus was carried out to produce high biomass yields to extract ON. K marxianus was grown for 20 h in medium containing 5% (w/v) dehydrated whey, at 30°C (pH 4.5), with agitation (350 rpm), and under aeration (1.0–2.0 vvm). After 20 h, media containing 10–15% (w/v) of dehydrated whey were added at different flow rates (180–230 ml/h). Samples were analyzed at 6–8 h intervals for cell count, lactose consumption, and ethanol production. Maximum production of biomass (28.13 g/l), yield (0.58 g/g), productivity (2.42 g/l per h), and specific growth rate (0.63 1/h) were obtained when medium containing 15% (w/v) of whey was added at 180 ml/h under 2 vvm aeration. Fed-batch fermentation converted 95% of whey lactose into biomass.     

Enhancement of glucose oxidase production in batch cultivation of recombinant Saccharomyces cerevisiae: optimization of oxygen transfer condition

AIMS: To obtain an optimal combination of agitation speed and aeration rate for maximization of specific glucose oxidase (GOD) production in recombinant Saccharomyces cerevisiae, and to establish a correlation between kLa vis-à-vis oxygen transfer condition and specific glucose oxidase production. METHODS AND RESULTS: The oxygen transfer condition was manifested indirectly by manipulating the impeller speed and aeration rate in accordance with a Central Composite Rotatory Design (CCRD). The dissolved oxygen concentration and the volumetric oxygen transfer coefficient (kLa) were determined at corresponding combinations of impeller speed and aeration rate. The maximal specific extracellular glucose oxidase production (3.17 U mg-1 dry cell mass) was achieved when the initial dissolved oxygen concentration was 6.83 mg l-1 at the impeller speed of 420 rev min-1 and at the rate of aeration of 0.25 vvm. It was found out that while impeller speed had a direct effect on the production of enzyme, a correlation between kLa and specific GOD production could not be established. CONCLUSION: At the agitation speed of 420 rev min-1 and at 0.25 vvm aeration rate, the degree of turbulence and the dissolved oxygen concentration were thought to be optimal both for cellular growth and production of enzyme. SIGNIFICANCE AND IMPACT OF THE STUDY: The combined effect of agitation and aeration on recombinant glucose oxidase production in batch cultivation has not yet been reported in the literature. Therefore, this study gives an insight into the effect of these two important physical parameters on recombinant protein production. It also suggests that since there is no correlation between kLa and specific production of GOD, kLa should not be used as one of the scale-up parameters.     

Batch and fed batch production of pectin lyase and pectate lyase by novel strain Debaryomyces nepalensis in bioreactor

The effect of various parameters such as pH, agitation and aeration was studied for maximum production of pectin lyase (PL) and pectate lyase (PGL) by a novel yeast strain Debaryomyces nepalensis in bioreactor. The optimal levels of pH, aeration and agitation rate was found to be 7.0, 300rpm and 1vvm, respectively. Under these conditions, D. nepalensis produced 14,200U/L of PL and 12,000U/L of PGL corresponding to a productivity of 600U/Lh and 500U/Lh of PL and PGL, respectively. Fed-batch production was studied by feeding inducer (lemon peel), carbon source (galactose) individually and in combination at 12h of growth for enhanced production of PL and PGL. Combined feeding of inducer and carbon source at 12h was found to be the best strategy for enhanced production of PL and PGL. Under these conditions, production of PL and PGL increased to 23,300U/L and 22,400U/L, respectively which corresponded to a productivity of 728U/Lh of PL and 700U/Lh of PGL, respectively. The production was increased by 1.6- and 1.8-fold and productivity by 1.2- and 1.4-fold for PL and PGL, respectively when compared to batch culture.     

High-level production of ethanol during fed-batch ethanol fermentation with a controlled aeration rate and non-sterile glucose powder feeding of Saccharomyces cerevisiae

In this study, we utilized a unique strategy for fed-batch fermentation using ethanol-tolerant Saccharomyces cerevisiae to achieve a high-level of ethanol production that could be practically applied on an industrial scale. During this study, the aeration rate was controlled at 0.0, 0.13, 0.33, and 0.8 vvm to determine the optimal aeration conditions for the production of ethanol. Additionally, non-sterile glucose powder was fed during fed-batch ethanol fermentation and corn-steep liquor (CSL) in the medium was used as an organic N-source. When aeration was conducted, the ethanol production and productivity were superior to that when aeration was not conducted. Specifically, the maximum ethanol production reached approximately 160 g/L, when the fermentor was aerated at 0.13 vvm. These findings indicate that the use of a much less expensive C-source may enable the fermentation process to be directed towards the improvement of overall ethanol production and productivity in fermentors that are aerated at 0.13 vvm. Furthermore, if a repeated fed-batch process in which the withdrawal and fill is conducted prior to 36 h can be employed, aeration at a rate of 0.33 and/or 0.8 vvm may improve the overall ethanol productivity     

通气量和菊粉浓度对克鲁维酵母乙醇发酵的影响

马克斯克鲁维酵母能够利用集成生物加工技术发酵菊芋生产乙醇,具有非粮燃料乙醇生产潜力.文中研究了该技术中的两个关键因素(通气量和底物浓度)对于K.marxinaus YX01乙醇发酵过程和菊粉酶活性的影响.研究结果表明,底物浓度对乙醇得率影响不大,底物浓度为250 g/L时,发酵终点乙醇浓度为84.74 g/L,但乙醇得率由低浓度50 g/L的86.4％(理论值),降为84.7％.通气能够加速K.marxinaus YX01的乙醇发酵过程,但降低了乙醇得率,当底物浓度为250 g/L时,乙醇得率由不通气的84.7％降为1.0 vvm时的73.3％.随底物浓度的升高及通气量的降低,K.marxinaus YX01分泌的菊粉酶活力表现出降低的趋势.在不通气及底物浓度为250 g/L时,菊粉酶的活性为6.59 U/mL,而底物浓度50 g/L,通气量1.0 vvm时的酶活力为21.54 U/mL.乙醇发酵过程中的副产物甘油随通气量的降低及底物浓度的升高而增大,而乙酸的浓度随通气量的增大及底物浓度的升高而升高.     

Antioxidant property and production of exopolysaccharide from Armillaria mellea in submerged cultures: Effect of culture aeration rate

Effects of culture aeration rate on production and antioxidant property of exopolysaccharide (EPS) by Armillaria mellea were investigated in a 5‐L stirred‐tank bioreactor where an optimal biomass aeration rate of 1.2 vvm with 0.22 g/g cell yield and 0.6 vvm EPS formation rate with 7.66 mg/g product yield were achieved. A two‐stage aeration process to maximize the biomass and EPS productions proceeded with a 1.55‐fold enhancement (from 4.28 to 6.65 g/L) in biomass formation and a 2.68‐fold enhancement (from 86.9 to 233.2 mg/L) in the EPS production, as compared with those from the aeration rate of 0.3 vvm. The molecular weights of EPS in cultures of different aeration rates are closely correlated with their protein/polysaccharide ratios (R²=0.830) and EC₅₀ (EC₅₀, the effective concentration where the antioxidant property is 50%) values in antioxidant activity (R²=0.960), reducing power (R²=0.894) and chelating ability (R²=0.954). EPS from the two‐stage aeration rate culture shows a strong antioxidant property by the conjugated diene method, reducing power and chelating ability on ions. Therefore, we present results to regulate and to optimize A. mellea cultures to efficiently produce biomass and EPS. The fermented EPS has the potential to be used as for antioxidant‐related functional foods and pharmaceutical industries.     

Production of human epidermal growth factor by an ampicillin resistant recombinant Escherichia coli strain

Summary The effect of medium composition and initial glucose concentration on production of hEGF by recombinant E. coli cells was investigated. Optimum hEGF production was observed in a yeast extract/acid hydrolysed casein/salts media containing an initial glucose concentration of 10 g.l^-1. A maximum hEGF titer of 250 mg.l^-1 was obtained in this medium after 32 h in laboratory fermenters with pH, temperature, agitation and aeration set at 6.8, 30°C, 500 rpm and 2 vvm, respectively.     

Isoforms of glucose 6-phosphate dehydrogenase in Deinococcus radiophilus

Glucose 6-phosphate dehydrogenase (G6PDH, EC 1.1.1.49) in Deinococcus radiophilus, an extraordinarily UV-resistant bacterium, was investigated to gain insight into its resistance as it was shown to be involved in a scavenging system of superoxide (O2-1) and peroxide (O2-2) generated by UV and oxidative stresses. D. radiophilus possesses two G6PDH isoforms: G6PDH-1 and G6PDH-2, both showing dual coenzyme specificity for NAD and NADP. Both enzymes were detected throughout the growth phase; however, the substantial increase in G6PDH-1 observed at stationary phase or as the results of external oxidative stress indicates that this enzyme is inducible under stressful environmental conditions. The G6PDH-1 and G6PDH-2 were purified 122- and 44-fold (using NADP as cofactor), respectively. The purified G6PDH-1 and G6PDH-2 had the specific activity of 2,890 and 1,033 U/mg protein (using NADP as cofactor) and 3,078 and 1,076 U/mg protein (using NAD as cofactor), respectively. The isoforms also evidenced distinct structures; G6PDH-1 was a tetramer of 35 kDa subunits, whereas G6PDH-2 was a dimer of 60 kDa subunits. The pIs of G6PDH-1 and G6PDH-2 were 6.4 and 5.7, respectively. Both G6PDH-1 and G6PDH-2 were inhibited by both ATP and oleic acid, but G6PDH-1 was found to be more susceptible to oleic acid than G6PDH-2. The profound inhibition of both enzymes by beta-naphthoquinone-4-sulfonic acid suggests the involvement of lysine at their active sites. Cu2+ was a potent inhibitor to G6PDH-2, but a lesser degree to G6PDH-1. Both G6PDH-1 and G6PDH-2 showed an optimum activity at pH 8.0 and 30 degrees .     

Effects of Cultivation Parameters on the Morphology of Rhizopus arrhizus and the Lactic Acid Production in a Bubble Column Reactor

The use of filamentous Rhizopus for lactic acid production is facing a challenge due to its low yield mainly caused by the difficulty to control its morphology in submerged fermentation processes. This study was aimed at investigating the impacts of cultivation parameters on the morphology of Rhizopus arrhizus DAR 36017 and lactic acid production using waste potato starch in a laboratory scale bubble column reactor (BCR). The fungal morphology was significantly influenced by carbon sources, process pH, starch concentrations, sparger designs and aeration rates. The favorable morphology for lactic acid production was a freely dispersed small pellet, which was achieved under operation conditions at pH 5.0–6.0, starch concentrations of 60–120 g/L and aeration rates of 0.2–0.8 vvm using a sintered stainless steel disc sparger. Optimal cultivation conditions at pH 6.0 and an aeration rate of 0.4 vvm resulted in the formation of freely dispersed small pellets and 103.8 g/L lactic acid with a yield of 87 % from 120 g/L liquefied potato starch in 48 h. The overall results in terms of lactic acid yield and productivity are comparable to those reported in previous studies using immobilized Rhizopus cells in batch fermentations.     

Effects of rheological properties and mass transfer on plant cell bioreactor performance: production of tropane alkaloids

Volumetric mass transfer coefficients, K(L)a were measured over an aeration rate range from 0.1 to 1.0 vvm in a 1.2-L draft-tube-type airlift bioreactor for different Datura stramonium cell concentrations and correlated with superficial air velocity and rheological properties of the cell suspension. The measured K(L)a values (17-40 h(-1)) for a cell volume fraction of 0.2 (v/v) were approximately 2 times higher than those for the highest cell concentrations tested (cell volume fraction 0.7-0.8 v/v). Cell suspensions exhibited yield stress and pseudoplastic behavior. This behavior was described by the Casson model. The estimated yield stress values depended upon cell concentration with an exponent of 4.0. An empirical correlation based on the data for plant cell suspensions exhibiting yield stress was developed in order to determine aeration strategy for the plant cell cultivation in draft-tube-type airlift bioreactors: \documentclass{article}\pagestyle{empty}\begin{document}$$ {\rm K}_{\rm L} {\rm a} = {\rm A}({\rm U}_{{\rm gr}});{0.3} ({\rm \eta }_{{\rm eff}});{ - 0.4} $$\end{document} Aeration rates above 1.0 vvm caused a significant drop in cell yield and product content. Maximum growth and production were obtained at 0.6 vvm aeration. The cell and product yields obtained at 1.7 vvm were 2.8 times lower than the maximum values (25 g cell DW/L and 73.8 mg tropane alkaloid/L). The effects of the increased aeration rates on cell yield were also evaluated in terms of Reynolds stress. It was found that there was a relation between cell damage and the estimated Reynolds stress. The Reynolds stress estimated for the same aeration rate decreased with increasing cell concentration, suggesting that cells in the cultures at low cell concentrations are subjected to hydrodynamic damage. In the experiments with the cell cultures having a cell concentration of 0.3 (v/v), approximately 70% reduction in cell concentration was observed when the Reynolds stress was increased from 10 to 50 dyn/cm(2). (c) 1993 John Wiley & Sons, Inc.