High cell density fed-batch fermentation for the production of a microbial lipase

Extracellular lipase of the yeast Candida rugosa was produced via high cell density fed-batch fermentations using palm oil as the sole source of carbon and energy. Feeding strategies consisted of a pH-stat operation, foaming-dependent control and specific growth rate control in different experiments. Compared to foaming-dependent feeding and the pH-stat operation, the specific growth rate control of feeding proved to be the most successful. At the specific growth rate control set at 0.05 h⁻¹, the final lipase activity in the culture broth was the highest at ∼700 U L⁻¹. This was 2.6-fold higher than the final enzyme activity obtained at a specific growth rate control set at 0.15 h⁻¹. The peak enzyme concentration achieved using the best foaming-dependent control of feeding was around 28% of the peak activity attained using the specific growth rate control of feeding at 0.05 h⁻¹. Similarly, the peak enzyme concentration attained using the pH-stat feeding operation was a mere 9% of the peak activity attained by specific growth rate control of feeding at a set-point of 0.05 h⁻¹. Fed-batch fermentations were performed in a 2 L stirred-tank bioreactor (30 °C, pH 7) with the dissolved oxygen level controlled at 30% of air saturation.     

The enhancement of specific antibody production rate in glucose- and glutamine-controlled fed-batch culture

The concentration effects of certain amino acids (Asp, Ile, Leu, Lys, Met, Val, Phe and Gln which were highly consumed during cultivation), and glucose on cell growth and antibody productivity were investigated using dish culture. From these experiments, it was found that only glutamine enrichment enhanced the specific antibody production rate. The other amino acids described above did not affect either the specific growth rate or specific antibody production rate. Thus we investigated the quantitative effects of glutamine concentration in the range of 0.4∼33.3 mmol·1⁻¹ on kinetic parameters in fed-batch culture which kept both glucose and glutamine concentration constant. As a result the specific growth rate decreased with increase in glutamine concentration in the range larger than 20 mmol·1⁻¹. The specific antibody production rate had a maximum value at about 25 mmol·1⁻¹ glutamine concentration.     

Use of response surface methodology to optimize culture medium for production of lovastatin by Monascus ruber

Response surface methodology (RSM) was employed to study the effect of culture medium on the production of lovastatin in mixed solid-liquid state (or submerged) cultures by Monascus ruber. The maximal lovastatin yield (131 mg/L, average of three repeats) appeared at the region where the respective concentrations of rice powder, peptone, glycerin, and glucose were around 34.4 g/L, 10.8 g/L, 26.4 ml/L, and 129.2 g/L, respectively. The optimized medium resulted in a significant increase of lovastatin yield, as compared with that obtained by the fermentation of many other M. ruber species.     

Deciphering role of technical bioprocess parameters for bioethanol production using microalgae

Microalgae biomass is considered an important feedstock for biofuels and other bioactive compounds due to its faster growth rate, high biomass production and high biomolecules accumulation over first and second-generation feedstock. This research aimed to maximize the specific growth rate of fresh water green microalgae Closteriopsis acicularis, a member of family Chlorellaceae under the effect of pH and phosphate concentration to attain enhanced biomass productivity. This study investigates the individual and cumulative effect of phosphate concentration and pH on specific growth characteristics of Closteriopsis acicularis in autotrophic mode of cultivation for bioethanol production. Central-Composite Design (CCD) strategy and Response Surface Methodology (RSM) was used for the optimization of microalga growth and ethanol production under laboratory conditions. The results showed that high specific growth rate and biomass productivity of 0.342 day⁻¹ and 0.497 g L⁻¹ day⁻¹ respectively, were achieved at high concentration of phosphate (0.115 g L⁻¹) and pH (9) at 21st day of cultivation. The elemental composition of optimized biomass has shown enhanced elemental accumulation of certain macro (C, O, P) and micronutrients (Na, Mg, Al, K, Ca and Fe) except for nitrogen and sulfur. The Fourier transform infrared spectroscopic analysis has revealed spectral peaks and high absorbance in spectral range of carbohydrates, lipids and proteins, in optimized biomass. The carbohydrates content of optimized biomass was observed as 58%, with 29.3 g L⁻¹ of fermentable sugars after acid catalyzed saccharification. The bioethanol yield was estimated as 51 % g ethanol/g glucose with maximum of 14.9 g/L of bioethanol production. In conclusion, it can be inferred that high specific growth rate and biomass productivity can be achieved by varying levels of phosphate concentration and pH during cultivation of Closteriopsis acicularis for improved yield of microbial growth, biomass and bioethanol production.     

Modeling and optimization of hairy root growth in fed‐batch process

This article proposes a feeding strategy based on a kinetic model to enhance hairy roots growth. A new approach for modeling hairy root growth is used, considering that there is no nutrient limitation thanks to an appropriate feeding, and the intracellular pools are supposed to be always saturated. Thus, the model describes the specific growth rate from extracellular concentration of the major nutrients and nutrient uptakes depend on biomass growth. An optimized feeding strategy was determined thanks to the model to maintain the major nutrient levels at their optimum assuming optimal initial concentrations. The optimal feed rate is computed in open loop using kinetic model prediction or in closed loop using conductivity measurements to estimate biomass growth. Datura innoxia was chosen as the model culture system. Shake flask cultures were used to calibrate the model. Finally, cultures in bioreactor were performed to validate the model and the control laws. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Increasing batch-to-batch reproducibility of CHO-cell cultures using a model predictive control approach

By means of a model predictive control strategy it was possible to ensure a high batch-to-batch reproducibility in animal cell (CHO-cell) suspensions cultured for a recombinant therapeutic protein (EPO) production. The general control objective was derived by identifying an optimal specific growth rate taking productivity, protein quality and process controllability into account. This goal was approached indirectly by controlling the oxygen mass consumed by the cells which is related to specific biomass growth rate and cell concentration profile by manipulating the glutamine feed rate. Process knowledge represented by a classical model was incorporated into the model predictive control algorithm. The controller was employed in several cultivation experiments. During these cultivations, the model parameters were adapted after each sampling event to cope with changes in the process’ dynamics. The ability to predict the state variables, particularly for the oxygen consumption, led to only moderate changes in the desired optimal operational trajectories. Hence, nearly identical oxygen consumption profiles, cell and protein titers as well as sialylation patterns were obtained for all cultivation runs.     

A medium optimization strategy for improvement of growth and methane production by Methanobacterium thermoautotrophicum

Methanobacterium thermoautotrophicum, strain Hveragerdi, has been cultivated in a completely defined mineral salts medium, under strictly anaerobic conditions with CO₂ and H₂ as sole carbon and energy source, respectively. During optimization of the medium an iron limitation was identified that could not be overcome by the simple addition of iron—or iron complexed with nitrilotriacetate (NTA)—to the medium, due to the formation of insoluble FeS complexes. In order to define a medium optimization strategy, and to avoid laborious empirical optimization procedures, a theoretical model has been developed in order to describe the solubility of iron and other mineral species in the medium as a function of the concentration of sulfur and NTA. This model may be applied for the optimization of any medium component. With this information sulfide has been replaced by a combination of cysteine and thiosulphate in conjunction with a non-toxic reducing agent (titanium (III) citrate). Using this defined medium precipitation was avoided and an iron limitation was overcome resulting in a 5-fold improvement of the final biomass concentration from 2–3 g l⁻¹ to 11.2 g l⁻¹ together with a 2-fold increase (from 45 to almost 100%) in the conversion of CO₂ and H₂ to CH₄, even at gas flow rates as high as 6 l min⁻¹.     

Optimization of medium composition for the production of antimicrobial activity by Bacillus subtilis B38

An antimicrobial activity produced by Bacillus subtilis B38 was found to be effective against several bacteria, including pathogenic and spoilage microorganisms such as, Listeria monocytogenes, Salmonella enteridis, and clinical isolates of methicillin‐resistant Staphylococcus species. Nutrients such as carbon, nitrogen sources, and inorganic salts enhanced the production level of the antibacterial activity by B. subtilis B38. A first screening step showed that lactose, ammonium succinate, and manganese most influenced both cell growth and antibacterial activity production. These three factors varied at two levels in eight experiments using full factorial design. Results indicated that maximum cell growth (OD = 10.2) and maximum production of antibacterial activity (360 AU/mL) were obtained in a modified medium containing 1.5% (w/v) lactose, 0.15% (w/v) ammonium succinate, and 0.3 mg/L manganese. Depending on the indicator strain used, the antibacterial activity was 2‐ to 4‐fold higher in the modified culture medium than in TSB medium under the same conditions. Thin layer chromatography‐bioautography assay showed the presence of three active spots with R_f values of 0.47, 0.7, and 0.82 in TSB medium. However, the inhibition zone of two spots (R_f values of 0.7 and 0.82) was slightly larger in the modified medium. Moreover, a large zone of inhibition with an R_f value of 0.3, was observed in this modified medium, instead of the spot having an R_f value of 0.47. These results suggest that the nutrients act as environmental factors, quantitatively and qualitatively affecting the production of antibacterial compounds by B. subtilis B38. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

A robust fed-batch feeding strategy independent of the carbon source for optimal polyhydroxybutyrate production

A three-stage control strategy independent of the organic substrate was developed for automated substrate feeding in a two-phase fed-batch culture of Cupriavidus necator DSM 545 for the production of the biopolymer polyhydroxybutyrate (PHB). The optimal feeding strategy was determined using glucose as the substrate. A combined substrate feeding strategy consisting of exponential feeding and a novel method based on alkali-addition monitoring resulted in a maximal cell concentration in the biomass growth phase. In the PHB accumulation phase, a constant substrate feeding strategy based on the estimated amount of biomass produced in the first phase and a specific PHB accumulation rate was implemented to induce PHB under limiting nitrogen at different biomass concentrations. Maximal cell and PHB concentrations of 164 and 125 g/L were obtained when nitrogen feeding was stopped at 56 g/L of residual biomass; the glucose concentration was maintained within its optimal range. The developed feeding strategy was validated using waste glycerol as the sole carbon source for PHB production, and the three-stage control strategy resulted in a PHB concentration of 65.6 g/L and PHB content of 62.7% while keeping the glycerol concentration constant. It can thus be concluded that the developed feeding strategy is sensitive, robust, inexpensive, and applicable to fed-batch culture for PHB production independent of the carbon source.     

Use of response surface methodology to optimize culture medium for production of lipase with Candida sp. 99-125

Response surface methodology (RSM) was employed to optimize culture medium for production of lipase with Candida sp. 99-125. In the first step, a Plackett–Burmen design was used to evaluate the effects of different components in the culture medium. Soybean oil, soybean powder and K₂HPO₄ have significant influences on the lipase production. The concentrations of three factors were optimized subsequently using central composite designs and response surface analysis. The optimized condition allowed the production of lipase to be increased from 5000 to 6230 IU/ml in shake flask system. The lipase fermentation in 5 l fermenter reached 9600 IU/ml.     

A systematic approach to the validation of process control parameters for monoclonal antibody production in fed-batch culture of a murine myeloma

A systematic approach to the validation of control ranges of control parameters for a cell culture process producing a monoclonal antibody is described. Specifically, the structure and functional activity of a monoclonal IgG1 antibody produced at the outer limits of numerical ranges of fed-batch culture control parameters such as pH and temperature were examined, with the aim of providing assurance that antibody produced under varying culture conditions was of consistent quality based on a carefully defined set of specifications. An experimental design was created using a half-fractional factorial design for fed-batch culture incorporating half of the thirty two possible combinations of five selected control parameters at high and low levels. Statistical analysis of all data gathered from the study allowed an assessment of the effects of the process control parameters at either high or low outer limits on fed-batch culture response variables such as growth rate and specific antibody productivity. Measured values for the responses of growth rate and specific antibody productivity throughout this study ranged from 0.22-0.44 d(-1) and 6.4-32 microg monoclonal antibody/10(6) cells/d respectively. Analytical characterisation of monoclonal antibody purified from each fed-batch culture considered the purity, structure and biological activity of the glycoprotein. All antibody preparations were identical to each other and to the current antibody reference standard or control. Glycosylation analysis of certain samples from the study demonstrated that the distribution of glycoforms of the antibody was not affected by the varying process control conditions of the fed-batch cultures.     

Optimization of medium composition for the production of exopolysaccharides from Phellinus baumii Pilát in submerged culture and the immuno-stimulating activity of exopolysaccharides

Optimization of medium composition for the production of exopolysaccharides (EPS) from Phellinus baumii Pilát in submerged culture and the immuno-stimulating activity of EPS were carried out. Firstly, the medium components having significant effect on EPS production were screened out to be glucose, yeast extract and diammonium oxalate monohydrate by using a 2⁽⁷⁻³⁾ fractional factorial design. Secondly, the concentrations of the three factors were optimized using central composite design in response surface methodology. As results, a quadratic model was found to fit for EPS production, and the optimal medium composition was determined as following (g/l): 34.12 glucose, 4 peptone, 5.01 yeast extract, 0.88 diammonium oxalate monohydrate, 0.75 MgSO₄ and 1 KH₂PO₄ and 0.0075 thiamine (VB₁). A yield of 2.363 ± 0.04 g/l for EPS was observed in verification experiment. Finally, EPS from P. baumii Pilát was found to have direct immuno-stimulating activity in vitro on splenocyte proliferative response and acid phosphatase activity in peritoneal macrophages in a dose-dependent manner.     

发酵动力学教学释疑解难尝试

在发酵动力学课程教学中,针对菌体生长速率与菌体比生长速率、菌体实际生长得率系数(Yx/s)与理论生长得率系数(Ygs)、产物实际得率系数(Yp/s)与理论得率系数(Yps)、补料分批发酵中比生长速率调控等常见知识难点进行了释疑解难尝试,收到了较好的课堂教学效果。     

Improving intracellular production of recombinant protein in <Emphasis Type="Italic">Pichia pastoris</Emphasis> using an optimized preinduction glycerol-feeding scheme

High-cell-density production of recombinant growth hormone of Lateolabrax japonicus (rljGH) expressed intracellularly in Pichia pastoris was investigated. In the regular strategy of induction at a cell density of 160 g l⁻¹, short duration of intracellular rljGH accumulation (17 h) resulted in a low final cell density of 226 g l⁻¹. Thus, a novel strategy of induction at a cell density of 320 g l⁻¹ was investigated. In this strategy, the preinduction glycerol-feeding scheme had a significant effect on the post-induction production. Constant glycerol feeding led to a decrease of the specific rljGH production and specific production rate because of low preinduction specific growth rate. This decrease was avoided by exponential glycerol feeding to maintain a preinduction specific growth rate of 0.16 h⁻¹. The results from exponential glycerol feeding indicated that the rljGH production depended on the preinduction specific growth rate. Moreover, mixed feeding of methanol and glycerol during induction improved the specific production rate to 0.07 mg g⁻¹ h⁻¹ from 0.043 mg g⁻¹ h⁻¹. Consequently, both high cell density (428 g l⁻¹) and high rljGH production could be achieved by the novel strategy: growing the cells at the specific growth rate of 0.16 h⁻¹ to the cell density of 320 g l⁻¹ and inducing the expression by mixed feeding.     

Statistical medium optimization and DO-STAT fed-batch fermentation for enhanced production of tyrosine phenol lyase in recombinant Escherichia coli

Abstract

Tyrosine phenol lyase (TPL) is a robust biocatalyst for the production of L-dihydroxyphenylalanine (L-DOPA). The improvement of TPL production is conducive to the industrial potential. In this study, the optimization of culture medium of recombinant Escherichia coli harboring TPL from Fusobacterium nucleatum (Fn-TPL) was carried out. Sucrose and combination of yeast extract and peptone were selected as carbon and nitrogen source, respectively. Their optimal concentrations were determined by Box-Behnken design and the synergistic effect between yeast extract and peptone was found to be significant, with p-value < 0.05. The DO-STAT fed-batch fermentation under optimized culture condition was established and the oxygen level was fixed at 20%. Both the biomass and Fn-TPL activity were significantly increased, which were 35.6 g dcw/L and 12292 U/L, respectively. The results obtained significantly promote the industrial production of L-DOPA production.     

Enhancement of oleandrin production in suspension cultures of Nerium oleander by combined optimization of medium composition and substrate feeding

Abstract

Oleandrin has been identified as the most potent antitumor ingredient of the Mediterranean herb Nerium oleander L. A strategy for optimization of medium compositions and conditions was developed for enhanced oleandrin production in suspension cultures from leaf-origin explants of Nerium oleander. The cell suspension cultures were grown in various modifications of MS medium as a basal medium. The effects of different natural extracts, plant growth substances, carbon and nitrogen sources and phosphate on the growth and oleandrin accumulation were investigated as well as effect of light, pH, shaking speed and substrate feeding. The highest oleandrin yield was obtained when the nitrogen concentration was lowered to two-thirds and the phosphate concentration increased by two-thirds of that specified in the MS medium in the presence of 3% sucrose, coconut milk, indolebutyric acid and benzyladenine in concentrations of 1 and 2 mg l^?1, respectively. Lower pH and faster shaking speed favored oleandrin accumulation. Chemical feeding of progesterone and cholesterol boosted the oleandrin concentration to higher levels reaching 8.23±0.05 mg g^?1 dry weight. This was about 10-fold higher than that detected in field-grown plants using the same extraction and analytic conditions, and about 24-fold higher than that determined in control cultures with regular MS medium and without precursor feeding.     

Optimization of medium composition and culture conditions for agarase production by Agarivorans albus YKW-34

Effect of medium composition and culture conditions on agarase production by Agarivorans albus YKW-34 was investigated in shake flasks. The most suitable carbon source, nitrogen source, and culture temperature were agar, yeast extract, and 25 °C, respectively, for agarase production by one-factor-at-a-time design. The nutritional components of the medium and culture conditions were analyzed by Plackett–Burman design. Among the nine factors studied, agar, yeast extract, and initial pH had significant effects on agarase production (p < 0.05). The optimum levels of these key variables were further determined using a central composite design. The highest agarase production was obtained in the medium consisting of 0.23% agar and 0.27% yeast extract at initial pH 7.81. The whole optimization strategy enhanced the agarase production from 0.23 U/ml to 0.87 U/ml. The economic medium composition and culture condition as well as the dominant occupation of agarase with high activity in culture fluid enlighten the potential application of A. albus YKW-34 for the production of agarase.