Fed-batch cultivation of transgenic rice cells for the production of hCTLA4Ig using concentrated amino acids

RAmy3D promoter is capable of expressing high levels of recombinant proteins in response to the depletion of sugar in transgenic rice cell suspension cultures. For this reason, it is necessary to change the growth medium into sugar-free production medium to produce the target protein, human cytotoxic T-lymphocyte antigen 4-immunoglobulin (hCTLA4Ig), using the inducible RAmy3D promoter. Since the two-stage culture is a complex process to perform in large-scale, a fed-batch method was evaluated with the addition of concentrated amino acids before the depletion of sugar to induce hCTLA4Ig production. This fed-batch culture was found to be effective and the production of hCTLA4Ig was enhanced up to 1.2-fold compared to that of two-stage cultures with medium exchange. In addition, when this fed-batch culture was performed in a 15-l stirred-tank bioreactor, maximum hCTLA4Ig level was 76.5 mg l⁻¹ at day 10.     

Recombinant protein production in cultures of an Escherichia coli trp − strain

Fermentation conditions were developed in order to achieve simultaneously a high biomass concentration and high-level expression of a hybrid cI-human insulin B peptide gene. In our system, this hybrid gene is under control of the Escherichia coli trp promoter, in a trp ^– derivative strain of E. coli W3110. The dual role of tryptophan concentration on cellular growth and hybrid gene regulation was studied in 10-l batch fermentations. In the best batch conditions, a biomass concentration of 12 g dry weight/l can be obtained, and 0.53 g/l of cI-insulin B hybrid protein is produced. Tryptophan in the culture medium is consumed by the growing culture, until a level is reached that causes induction of the hybrid gene. Plasmid loss was detected, as only 62% of the cells retained the recombinant plasmid. In order to increase the hybrid protein production level, a fed-batch culture strategy was developed whereby the specific growth rate of the cells was restrained. Using the same amount of nutrients as in the batch fermentations, it was possible to increase the final biomass concentration to 20 g/l, plasmid-bearing cells in the population to 90% and recombinant hybrid protein to 1.21 g/l. Correspondence to: F. Bolivar     

Fed-batch cultures of recombinant Escherichia coli with inhibitory substance concentration monitoring

Fed-batch cultures of recombinant Escherichia coli HB101 were investigated to obtain high cell density and large amounts of β-galactosidase (β-gal). E. coli HB1010 was transformed with a hybrid plasmid pTREZ1, which contained a β-gal gene controlled by the trp promoter. In fed-batch cultures of recombinant E. coli, when the cell concentration reached around 13 g/l, the cell growth stopped and large amounts of inhibitory substances have accumulated in the broth. These inhibitory substances were isolated and identified. Acetate produced by the cells was evidently the main inhibitor of cell growth and β-gal production. Since the cells proved to assimilate acetate, the feed rate was controlled with acetate concentration monitoring in the fed-batch culture. As a result, the acetate concentration was maintained at a low level and cells grew smoothly without acetate-induced inhibition. Cell concentration and β-gal quantity reached high values of 28 g/l and 64 U/ml, respectively.     

Production of thuringiensin by fed-batch culture of Bacillus thuringiensis subsp. darmstadiensis 032 with an improved pH-control glucose feeding strategy

A improved pH-control fed-batch strategy for Bacillus thuringiensis subsp. darmstadiensis 032 producing thuringiensin was developed based on the analysis of the batch culture, constant rate fed-batch cultures and the original pH-control fed-batch. Having considered the pH variation and the glucose consumption status, the pH was adjusted from 6.5 to 7.0 by adding base in the late cultivation period of batch culture, and then the pH was kept at 7.0 by glucose feeding. The feeding was terminated when the pH could not be controlled by glucose feeding anymore. The proposed fed-batch strategy effectively avoided underfeeding or overfeeding, and it increased the thuringiensin yield and Y_P/X by 89.51% and 103.2% compared to that of the batch culture, respectively.     

Development and optimization of two-stage cyclic fed-batch culture for hG-CSF production using L-arabinose promoter of Escherichia coli

The long-term process for producing human granulocyte-colony stimulating factor (hG-CSF) was developed using two-stage cyclic fed-batch culture, in which hG-CSF expressing-recombinant Escherichia coli was directed by an L-arabinose promoter system. For the optimization, the preinduction growth rate during the growth stage and the feeding strategy during the production stage were investigated. The maximum harvest volume during the production stage was predicted before long-term cyclic operation. Based on those optimized strategies, the two-stage cyclic fed-batch culture was performed for 12 cycles (86 h). The cell growths in both stages were maintained at 45-50 g/L and 71-77 g/L, respectively. hG-CSF was stably produced at a level of 8-9 g/L and the plasmid stability was maintained at more than 90%. Volumetric productivity by the two-stage cyclic fed-batch culture was 0.643 g/L/h, which was about 280% higher than that of conventional DO-stat fed-batch culture.     

Fed-batch operation in special microtiter plates: a new method for screening under production conditions

Batch and fed-batch operation result in completely different physiological conditions for cultivated microorganisms or cells. To close the gap between screening, which is hitherto exclusively performed in batch mode, and fed-batch production processes, a special microtiter plate was developed that allows screening in fed-batch mode. The fed-batch microtiter plate (FB-MTP) enables 44 parallel fed-batch experiments at small scale. A small channel filled with a hydrogel connects a reservoir well with a culture well. The nutrient compound diffuses from the reservoir well through the hydrogel into the culture well. Hence, the feed rate can easily be adjusted to the needs of the cultured microorganisms by changing the geometry of the hydrogel channel and the driving concentration gradient. Any desired compound including liquid nutrients like glycerol can be fed to the culture. In combination with an optical measuring device (BioLector), online monitoring of these 44 fed-batch cultures is possible. Two Escherichia coli strains and a Hansenula polymorpha strain were successfully cultivated in the new FB-MTP. As a positive impact of the fed-batch mode on the used strains, a fourfold increase in product formation was observed for E. coli. For H. polymorpha, the use of fed-batch mode resulted in a strong increase in product formation, whereas no measurable product formation was observed in batch mode. In conclusion, the newly developed fed-batch microtiter plate is a versatile, easy-to-use, disposable system to perform fed-batch cultivations at small scale. Screening cultures in high-throughput under online monitoring are possible similar to cultivations under production conditions.     

Nuclear factors GT-1 and 3AF1 interact with multiple sequences within the promoter of the Tdc gene from Madagascar periwinkle: GT-1 is involved in UV light-induced expression

Plant secondary metabolites of the terpenoid indole alkaloid (TIA) class comprise several compounds with pharmaceutical applications. A key step in the TIA biosynthetic pathway is catalysed by the enzyme tryptophan decarboxylase (TDC), which channels the primary metabolite tryptophan into TIA metabolism. In Catharanthus roseus (Madagascar periwinkle), the Tdc gene is expressed throughout plant development. Moreover, Tdc gene expression is induced by external stress signals, such as fungal elicitor and UV light. In a previous study of Tdc promoter architecture in transgenic tobacco it was shown that the ?538 to ?112 region is a quantitative determinant for the expression level in different plant organs. Within this sequence one particular region (?160 to ?99) was identified as the major contributor to basal expression and another region (?99 to ?37) was shown to be required for induction by fungal elicitor. Here, the in vitro binding of nuclear factors to the ?572 to ?37 region is described. In extracts from tobacco and C. roseus, two binding activities were detected that could be identified as the previously described nuclear factors GT-1 and 3AF1, based on their mobility and binding characteristics. Both factors appeared to interact with multiple regions in the Tdc promoter. Mutagenesis of GT-1 binding sites in the Tdc promoter did not affect the basal or elicitor-induced expression levels. However, induction of the Tdc promoter constructs by UV light was significantly lower, thereby demonstrating a functional role for GT-1 in the induction of Tdc expression by UV light.     

Ethanol effect on batch and fed-batch Arthrospira platensis growth

The ability of Arthrospira platensis to use ethanol as a carbon and energy source was investigated by batch process and fed-batch process. A. platensis was cultivated under the effect of a single addition (batch process) and a daily pulse feeding (fed-batch process) of pure ethanol, at different concentrations, to evaluate cell concentration (X) and specific growth rate (μ). A marked increase was observed in the cell concentration of A. platensis in runs with ethanol addition when compared to control cultures without ethanol addition. The fed-batch process using an ethanol concentration of 38 mg L^?1 days^?1 reached the maximum cell concentration of 2,393 ± 241 mg L^?1, about 1.5-fold that obtained in the control culture. In all experiments, the maximum specific growth rate was observed in the early exponential phase of cell growth. In the fed-batch process, μ decreased more slowly than in the batch process and control culture, resulting in the highest final cell concentration. Ethanol can be used as a feasible carbon and energy source for A. platensis growth via a fed-batch process.     

Nutrient control by the gas evolution in methanogenesis of methanol by Methanosarcina barkeri

A practical fed-batch culture, in which consumed amounts of methanol and other nutrients were supplied in response to a direct signal of the gas production of CH₄ and CO₂, was carried out for the cell production of methanol-utilizing Methanosarcina barkeri. In this fed-batch culture system equipped with level sensors to detect the gas production, a high cell concentration of 24.4 g/l was attained in 175-h cultivation maintaining the optimized nutrient concentrations of methanol, NH₄⁺, PO₄³⁻, Na⁺, Mg²⁺, Ca²⁺, Fe²⁺, Ni²⁺, Co²⁺ and cysteine (S source) throughout the culture.     

Peroxidase production by carbon and nitrogen sources fed-batch culture of Arthromyces ramosus

Summary Carbon and nitrogen sources were investigated for improving peroxidase production by Arthromyces ramosus, a hyperproducer of peroxidase. Glucose as carbon source and a mixture of yeast extract and polypeptone at the ratio of 3 to 5 as nitrogen source in a production medium were shown to give the highest peroxidase activity. During the culture amino acids such as alanine, arginine, methionine, leucine, tyrosine and tryptophan were depleted. Therefore, glucose supplemented nitrogen source fed-batch culture was carried out and a peroxidase activity of 73 U/ml was obtained. This activity was 1.7 times higher than that of glucose fed-batch culture. This indicates that an adequate nitrogen source supply during the culture is effective for improving the peroxidase production by A. ramosus.     

Fed-batch sorbitol to sorbose fermentation by A. suboxydans

Batch kinetics for sorbitol to sorbose bioconversion was studied at 20% sorbitol concentration. The culture featured 90% conversion of sorbitol to sorbose in 20 hours. Increasing the initial substrate concentration in the bioreactor decreased the culture specific growth rate. At 40% initial sorbitol concentration no culture growth was observed. The batch kinetics and substrate inhibition studies were used to develop the Mathematical Model of the system. The model parameters were identified using the original batch kinetic data (S _o =20%). The developed mathematical model was adopted to fed-batch cultivation with the exponential nutrient feeding. The fed-batch model was simulated and implemented experimentally. No substrate inhibition was observed in the fed-batch mode and it provided an overall productivity of 12.6?g/l-h. The fed-batch model suitably described the experimentally observed results. The model is ready for further optimization studies.     

Enhanced production of α-ketoglutarate by fed-batch culture in the metabolically engineered strains of Corynebacterium glutamicum

The fed-batch culture system was employed to enhance production of α-ketoglutarate (α-KG) by the strainsof Corynebacterium glutamicum, whose genes encoding the key enzymes responsible for the biosynthesis of L-glutamate from α-KG were deleted. In a shake flask fermentation, C. glutamicum JH110 in which the 3 genes, gdh (encoding glutamate dehydrogenase), gltB (encoding glutamate synthase), and aceA (encoding isocitrate lyase) were disrupted showed the highest production of α-KG (12.4 g/L) compared to the strains JH102 (gdh mutant), JH103 (gltB mutant), and JH107 (gdh gltB double mutant). In the fed-batch cultures using a 5 L-jar fermenter, the strain JH107 produced more α-KG (19.5 g/L), but less glutamic acid (23.3 g/L) than those produced by the parent strain HH109, as well as JH102. The production of α-KG was significantly enhanced and the accumulation of glutamicacid was minimized by the ammonium-limited fed-batch cultures employing C. glutamicum JH107. Further improvement of α-KG production by the strain JH107 was achieved through the ammonium-limited fed-batch culture with the feeding of molasses, and the levels of α-KG and glutamic acid produced were 51.1 and 0.01 g/L, respectively.     

Production of a recombinant, immunogenic protein, P64k, of Neisseria meningitidis in Escherichia coli in fed-batch fermenters

P64k is a Neisseria meningitidis high molecular weight protein present in meningococcal vaccine preparations. The lpdA gene, codifying for this protein, was cloned in Escherichia coli and the P64k protein was expressed in Escherichia coli K12 W3110 under the control of the tryptophan promoter. The recombinant bacteria were grown in batch or fed-batch cultures. P64k was expressed as an intracellular soluble form at about 40% of the total cellular protein. A final productivity of 215 mg l^–1 h^–1 and 11 g cell dry wt l^–1 were obtained when the fed-batch culture conditions were optimised, compared to 30% of total protein, and a productivity of 76 mg l^–1 h^–1 and 5.1 g cell dry wt l^–1 in batch cultivation.     

A simple feedback control of Escherichia coli growth for recombinant aldolase production in fed-batch mode

Fed-batch production of recombinant fuculose-1-phosphate aldolase (FucA) by Escherichia coli XL1 Blue MRF′ (pTrcfuc) has been automated by using a simple feedback specific growth rate control strategy. Non-induced continuous cultures were conducted in order to characterize substrate consumption and carbon dioxide production yields and rates. In fed-batch cultures, substrate feeding rate was adjusted using on-line biomass estimation based on exhaust gas analysis and macroscopic mass balances. Overexpression of recombinant protein induced by isopropyl-β-d-thiogalactopyranoside (IPTG) under trc promoter did not affect significantly the control of specific growth rate during 7 h after induction. Growth and protein production curves were parallel until high level of protein expression started to inhibit cell growth. The proposed specific growth rate control strategy has been successfully applied to both non-induced and induced fed-batch cultures that do not exhibit severe growth rate depression.     

Genetic evidence for a positive-acting regulatory factor mediating induction in the tryptophan pathway of Pseudomonas aeruginosa

A series of deletions of most or all of trpA, the distal member of the Pseudomonas aeruginosa tryptophan synthase structural gene pair, was constructed by BAL31 nuclease digestion and religation of a suitable plasmid. The residual trpB gene showed normal regulation, virtually ruling out the hypothesis of autogenous regulation proposed earlier on the basis of indirect evidence. On the other hand, SacII-mediated deletion of either or both of two small segments upstream from the trpBA promoter resulted in a fixed, low level of expression of the tryptophan synthase genes. Complementation studies implicated this region as the source of a diffusable, positive-acting regulatory factor responsible for the induction of the tryptophan synthase genes by their substrate, indoleglycerol phosphate.     

In Vitro Growth of Curcuma longa L. in Response to Five Mineral Elements and Plant Density in Fed-Batch Culture Systems

Plant density was varied with P, Ca, Mg, and KNO₃ in a multifactor experiment to improve Curcuma longa L. micropropagation, biomass and microrhizome development in fed-batch liquid culture. The experiment had two paired D-optimal designs, testing sucrose fed-batch and nutrient sucrose fed-batch techniques. When sucrose became depleted, volume was restored to 5% m/v sucrose in 200 ml of modified liquid MS medium by adding sucrose solutions. Similarly, nutrient sucrose fed-batch was restored to set points with double concentration of treatments’ macronutrient and MS micronutrient solutions, along with sucrose solutions. Changes in the amounts of water and sucrose supplementations were driven by the interaction of P and KNO₃ concentrations. Increasing P from 1.25 to 6.25 mM increased both multiplication and biomass. The multiplication ratio was greatest in the nutrient sucrose fed-batch technique with the highest level of P, 6 buds/vessel, and the lowest level of Ca and KNO₃. The highest density (18 buds/vessel) produced the highest fresh biomass at the highest concentrations of KNO₃ and P with nutrient sucrose fed-batch, and moderate Ca and Mg concentrations. However, maximal rhizome dry biomass required highest P, sucrose fed-batch, and a moderate plant density. Different media formulations and fed-batch techniques were identified to maximize the propagation and storage organ responses. A single experimental design was used to optimize these dual purposes.     

A novel fed-batch based strategy for enhancing cell-density and recombinant cyprosin B production in bioreactors

Nowadays, the dairy industry is continuously looking for new and more efficient clotting enzymes to create innovative products. Cyprosin B is a plant aspartic protease characterized by clotting activity that was previously cloned in Saccharomyces cerevisiae BJ1991 strain. The production of recombinant cyprosin B by a batch and fed-batch culture was compared using glucose and galactose as carbon sources. The strategy for fed-batch cultivation involved two steps: in the first batch phase, the culture medium presented glucose 1 % (w/v) and galactose 0.5 % (w/v), while in the feed step the culture medium was constituted by 5 % (w/v) galactose with the aim to minimize the GAL7 promoter repression. Based on fed-batch, in comparison to batch growth, an increase in biomass (6.6-fold), protein concentration (59 %) and cyprosin B activity (91 %) was achieved. The recombinant cyprosin B was purified by a single hydrophobic chromatography, presenting a specific activity of 6 × 10⁴ U·mg^?1, corresponding to a purification degree of 12.5-fold and a recovery yield of 16.4 %. The SDS-PAGE analysis showed that recovery procedure is suitable for achieving the purified recombinant cyprosin B. The results show that the recombinant cyprosin B production can be improved based on two distinct steps during the fed-batch, presenting that this strategy, associated with a simplified purification procedure, could be applied to large-scale production, constituting a new and efficient alternative for animal and fungal enzymes widely used in cheese making.     

Pullulan production by a non-pigmented strain of Aureobasidium pullulans using batch and fed-batch culture

The production of pigment-free pullulan by Aureobasidium pullulans in batch and fed-batch culture was investigated. Batch culture proved to be a better fermentation system for the production of pullulan than the fed-batch culture system. A maximum polysaccharide concentration (31.3 g l⁻¹), polysaccharide productivity (4.5 g l⁻¹ per day), and sugar utilization (100%) were obtained in batch culture. In fed-batch culture, feed medium composition influenced the kinetics of fermentation. For fed-batch culture, the highest values of pullulan concentration (24.5 g l⁻¹) and pullulan productivity (3.5 g l⁻¹ per day) were obtained in culture grown with feeding substrate containing 50 g l⁻¹ sucrose and all nutrients. The molecular size of pullulan showed a decline as fermentation progressed for both fermentation systems. At the end of fermentation, the polysaccharide isolated from the fed-batch culture had a slightly higher molecular weight than that of batch culture. Structural characterization of pullulan samples (methylation and enzymic hydrolysis with pullulanase) revealed the presence of mainly α-(1→4) (∼66%) and α-(1→6) (∼31%) glucosidic linkages; however, a small amount (<3%) of triply linked (1,3,4-, 1,3,6-, 1,2,4- and 1,4,6-Glc p) residues were detected. The molecular homogeneity of the alcohol-precipitated polysaccharides from the fermentation broths as well as the structural features of pullulan were confirmed by ¹³C-NMR and pullulanase treatments followed by gel filtration chromatography of the debranched digests.     

Comparative mycelial and spore yield by Trichoderma viride in batch and fed-batch cultures

The effects of cultural parameters such as carbon and nitrogen source and environmental factors including temperature and pH were investigated on spore and mycelial yield of Trichoderma viride, which has potential as a biocontrol agent against species of Fusarium in batch culture and fed-batch culture where there was limiting nutrient. The results obtained indicated that growth and sporulation of T. viride were greatly influenced by various carbon and nitrogen sources, and by environmental factors such as pH and temperature. Mannitol, wheat bran and rice bran as sole carbon sources appear to stimulate high mycelial growth and spore yield in fed-batch culture. Growth and sporulation were also favoured by NaNO₃, peptone and NH₄SO₄ as the nitrogen sources in fed-batch and batch cultures_. Maximum growth and sporulation was between pH 4.5 and 6.0. Temperatures between 30 and 37 °C were good for mycelium growth of T. viride while temperatures between 30 to 45 °C were good for sporulation. The amount of spore and mycelium produced and the time required for attainment of maximum spore yield increased with increasing carbon and nitrogen source in batch culture. The final spore yield obtained in fed-batch culture was two times higher than the apparent spore-carrying capacity of batch culture. These results show that T. viride is capable of growing and sporulating with varied nutritional and environmental conditions, and, therefore, this strain of T. viride may be useful as a biocontrol agent under diverse physiological and environmental conditions.