Increase In Volumetric Productivity Research Articles

Comprehensive metabolomics reveals correlation between sophorolipid biosynthesis and autophagy

Sophorolipids are biobased and biodegradable glycolipid surface-active agents contributing to the shift from petroleum to biobased surfactants, associated with clear environmental benefits. However, their production cost is currently too high to allow commercialisation. Therefore, a continuous sophorolipid production process was evaluated, i.e., a retentostat with an external filtration unit. Despite an initial increase in volumetric productivity, productivity eventually declined to almost 0 g L−1 h−1. Following comprehensive metabolomics on supernatant obtained from a standardised retentostat, we hypothesised exhaustion of the N-starvation-induced autophagy as the main mechanism responsible for the decline in bolaform sophorolipid productivity. Thirty-six metabolites that correlate with RNA/protein autophagy and high sophorolipid productivity were putatively identified. In conclusion, our results unveil a plausible cause of this bola sophorolipid productivity decline in an industrially relevant bioreactor set-up, which may thus impact majorly on future yeast biosurfactant regulation studies and the finetuning of bola sophorolipid production processes.

Combining Metabolic Engineering and Multiplexed Screening Methods for 3-Hydroxypropionic Acid Production in Pichia pastoris.

Production of 3-hydroxypropionic acid (3-HP) in Pichia pastoris (syn. Komagataella phaffii) via the malonyl-CoA pathway has been recently demonstrated using glycerol as a carbon source, but the reported metrics were not commercially relevant. The flux through the heterologous pathway from malonyl-CoA to 3-HP was hypothesized as the main bottleneck. In the present study, different metabolic engineering approaches have been combined to improve the productivity of the original 3-HP producing strains. To do so, an additional copy of the gene encoding for the potential rate-limiting step of the pathway, i.e., the C-terminal domain of the malonyl-CoA reductase, was introduced. In addition, a variant of the endogenous acetyl-CoA carboxylase (ACC1 S1132A ) was overexpressed with the aim to increase the delivery of malonyl-CoA. Furthermore, the genes encoding for the pyruvate decarboxylase, aldehyde dehydrogenase and acetyl-CoA synthase, respectively, were overexpressed to enhance conversion of pyruvate into cytosolic acetyl-CoA, and the main gene responsible for the production of the by-product D-arabitol was deleted. Three different screening conditions were used to classify the performance of the different strains: 24-deep-well plates batch cultures, small-scale cultures in falcon tubes using FeedBeads® (i.e., slow release of glycerol over time), and mini bioreactor batch cultures. The best two strains from the FeedBeads® screening, PpHP8 and PpHP18, were tested in bioreactor fed-batch cultures using a pre-fixed exponentially increasing feeding rate. The strain PpHP18 produced up to 37.05 g L−1 of 3-HP at 0.712 g L−1 h−1 with a final product yield on glycerol of 0.194 Cmol−1 in fed-batch cultures. Remarkably, PpHP18 did not rank among the 2-top producer strains in small scale batch cultivations in deep-well plates and mini bioreactors, highlighting the importance of multiplexed screening conditions for adequate assessment of metabolic engineering strategies. These results represent a 50% increase in the product yield and final concentration, as well as over 30% increase in volumetric productivity compared to the previously obtained metrics for P. pastoris. Overall, the combination of glycerol as carbon source and a metabolically engineered P. pastoris strain resulted in the highest 3-HP concentration and productivity reported so far in yeast.

Relationships between spacing, productivity and profitability of eucalypt plantations in a small rural property in south-eastern Brazil

Tree cultivation spacing can influence productivity and wood quality, with silvicultural, technological and economic implications. This study aimed to estimate the production and provide an economic analysis of Eucalyptus urophylla × Eucalyptus grandis stands as a function of planting spacing in a small rural property. The study was carried out in the Zona da Mata of Minas Gerais state, with the hybrid clone (GG100) established in 2 × 1 m, 2 × 2 m, 3 × 2 m and 3 × 3 m spacing. Inventories were carried out at 14, 54 and 84 months in four plots from each spacing, with 24 plants. Diameter at breast height (DBH), total height and survival rate were evaluated. The study evaluated the logistic model of growth and yield for the different spacings and analysed production costs, characterising the expenditure elements related to inputs and labour. For the economic analysis, we considered a discount rate of 8% p.a. and the valuation methods of net present value (NPV), annual equivalent value (AEV), average production cost (APC), and cost–benefit ratio (CBR). Spacing influenced diameter distribution, tree height and productivity. The optimal harvest age showed a tendency to decrease in smaller spacing. The increase in plant density (smaller spacing) did not promote a proportional increase in volumetric production. Our results indicated economic viability from 60 months onwards for all spacing, except for 2 × 1 m.

From chemostats to high‐density perfusion: the progression of continuous mammalian cell cultivation

AbstractContinuous cultivation of mammalian cells originated in chemostats in the 1950s and, through a series of technological advancements, has evolved into modern‐day high‐density perfusion processes with volumetric productivities >5 g L–1 day–1over extended cultivation periods. With appropriate process development, these productivities can be achieved with no adverse impact on cell line stability and product quality. Developments in downstream processing and automation have enabled the integration of drug substance manufacturing processes suitable for next‐generation plants that require lower capital deployment, with the potential for rapid construction and validation for clinical and commercial production. Perfusion also has been successfully used to generate high‐density cell banks (> 50 × 106cells mL–1) and for seed‐train optimization. They have resulted in significant productivity increases (10‐fold increase in volumetric productivity) from fed‐batch bioreactors by providing a high‐density seeding culture that elevates the inoculation density in a production bioreactor (> 5 × 106cells mL–1). Related advancements in cell culture medium formulations and cell line performance typically are independent of bioreactor format and have broad applicability for biotherapeutic manufacturing. The last decade has seen renewed interest in high‐density perfusion cultures and technological advances spanning the entire space of drug substance manufacturing – from cell line development to the final purification step. Continually evolving, these new technologies now are being introduced into clinical and commercial manufacturing. We anticipate that the general principles and knowledge gleaned from process intensification will extend well beyond classical perfusion cultivation and into all aspects of mammalian cell culture. © 2021 Society of Chemical Industry (SCI).

Reduced viscosity mutants of Trichoderma reesei with improved industrial fermentation characteristics.

Morphological mutants of Trichoderma reesei were isolated following chemical or insertional mutagenesis. The mutant strains were shown to have reduced viscosity under industrially relevant fermentation conditions and to have maintained high specific productivity of secreted protein. This allowed higher biomass concentration to be maintained during the production phase and, consequently, increased volumetric productivity of secreted protein. The causative mutations were traced to four individual genes (designated sfb3, ssb7, seb1, and mpg1). We showed that two of the morphological mutations could be combined in a single strain to further reduce viscosity and enable a 100% increase in volumetric productivity.

Reduction of medium consumption in perfusion mammalian cell cultures using a perfusion rate equivalent concentrated nutrient feed

Media preparation for perfusion cell culture processes contributes significantly to operational costs and the footprint of continuous operations for therapeutic protein manufacturing. In this study, definitions are given for the use of a perfusion equivalent nutrient feed stream which, when used in combination with basal perfusion medium, supplements the culture with targeted compounds and increases the medium depth. Definitions to compare medium and feed depth are given in this article. Using a concentrated nutrient feed, a 1.8-fold medium consumption (MC) decrease and a 1.67-fold increase in volumetric productivity (PR) were achieved compared to the initial condition. Later, this strategy was used to push cell densities above 100 × 106 cells/ml while using a perfusion rate below 2 RV/day. In this example, MC was also decreased 1.8-fold compared to the initial condition, but due to the higher cell density, PR was increased 3.1-fold and to an average PR value of 1.36 g L-1 day-1 during a short stable phase, and versus 0.46 g L-1 day-1 in the initial condition. Overall, the performance improvements were aligned with the given definitions. This multiple feeding strategy can be applied to gain some flexibility during process development and also in a manufacturing set-up to enable better control on nutrient addition.

Towards in situ continuous feeding via controlled release of complete nutrients for fed-batch culture of animal cells

Small-scale culture of animal cells in suspension is of importance for many applications. At a small-scale, fed-batch is achieved either by manual bolus feeding or the use of liquid handling robots. In this study, we report an alternate application of a hydrogel for in situ continuous delivery of a nutrient feed comprising 18 amino acids, vitamins, antioxidants, and trace elements. We show that amino acid release is sustained for at least seven days. Importantly, release rates of individual amino acids can be independently modulated by changing their loading. We demonstrate the application of this hydrogel for complete in situ feeding of nutrients to a suspension adapted CHO cell line expressing IgG leading to 2.7-fold and 4-fold improvement in integral viable cell density (IVCD) and volumetric productivity respectively. This is similar to improvements obtained by bolus liquid feeding. Further, supplying glucose from the same hydrogel to eliminate manual feeding led to a 1.8-fold increase in IVCD accompanied by a 3-fold increase in volumetric productivity as compared to batch culture. In summary, this study provides a proof-of-concept that hydrogels can enable completely closed in situ feeding for mammalian cell culture requiring no external intervention. Such continuous in situ delivery can potentially enable closed culture systems maintaining nutrients at low levels mimicking physiological concentrations.

Metabolic modeling and response surface analysis of an Escherichia coli strain engineered for shikimic acid production

BackgroundClassic metabolic engineering strategies often induce significant flux imbalances to microbial metabolism, causing undesirable outcomes such as suboptimal conversion of substrates to products. Several mathematical frameworks have been developed to understand the physiological and metabolic state of production strains and to identify genetic modification targets for improved bioproduct formation. In this work, a modeling approach was applied to describe the physiological behavior and the metabolic fluxes of a shikimic acid overproducing Escherichia coli strain lacking the major glucose transport system, grown on complex media.ResultsThe obtained flux distributions indicate the presence of high fluxes through the pentose phosphate and Entner-Doudoroff pathways, which could limit the availability of erythrose-4-phosphate for shikimic acid production even with high flux redirection through the pentose phosphate pathway. In addition, highly active glyoxylate shunt fluxes and a pyruvate/acetate cycle are indicators of overflow glycolytic metabolism in the tested conditions. The analysis of the combined physiological and flux response surfaces, enabled zone allocation for different physiological outputs within variant substrate conditions. This information was then used for an improved fed-batch process designed to preserve the metabolic conditions that were found to enhance shikimic acid productivity. This resulted in a 40% increase in the shikimic acid titer (60 g/L) and 70% increase in volumetric productivity (2.45 gSA/L*h), while preserving yields, compared to the batch process.ConclusionsThe combination of dynamic metabolic modeling and experimental parameter response surfaces was a successful approach to understand and predict the behavior of a shikimic acid producing strain under variable substrate concentrations. Response surfaces were useful for allocating different physiological behavior zones with different preferential product outcomes. Both model sets provided information that could be applied to enhance shikimic acid production on an engineered shikimic acid overproducing Escherichia coli strain.

Optimization of Herbicidin A Production in Submerged Culture of Streptomyces scopuliridis M40.

Herbicidin A is a potent herbicide against dicotyledonous plants as well as an antibiotic against phytopathogens. In this study, fermentation parameters for herbicidin A production in submerged culture of Streptomyces scopuliridis M40 were investigated. The herbicidin A concentration varied with the C/N ratio. High C/N ratios (>4) resulted in a herbicidin A production of more than 900 mg/l, whereas maximally 600 mg/l was obtained at ratios between 1 and 3.5. In 5-L batch fermentation, there was a positive correlation between the oxygen uptake rate (OUR) and herbicidin A production. Once the OUR increased, the substrate consumption rate increased, leading to an increase in volumetric productivity. Mechanical shear force affected the hyphal morphology and OUR. When the medium value of hyphal size ranged from 150 to 180 μm, high volumetric production of herbicidin A was obtained with OUR values >137 mg O2/l·h. The highest herbicidin A concentration of 956.6 mg/l was obtained at 500 rpm, and coincided with the highest relative abundance of hyphae of 100-200 μm length and the highest OUR during cultivation. Based on a constant impeller tip speed, which affects hyphal morphology, herbicidin A production was successfully scaled up from a 5-L jar to a 500-L pilot vessel.

Process strategies for enhancing recombinant streptokinase production in Lactococcus lactis cultures using P170 expression system

The production of recombinant proteins in Lactococcus lactis is often limited by several process and biological constraints. Recombinant gene expression in the P170 system of L. lactis is triggered at a pH below 6.5 by lactic acid accumulation. This work has used static flask, batch bioreactor and chemostat studies to independently investigate various factors affecting production of recombinant streptokinase. These factors are induction strength, complex-nutrient supplementation, specific growth rate and the cellular response to acid-stress termed as acid tolerance response (ATR). In the P170 system, induction strength is mainly a function of lactate concentration. Recombinant protein production is enhanced by increasing induction strength and complex-nutrient supplementation. However, acid-induced cellular stress-response has a deleterious effect on recombinant protein productivity. It is seen that suppression of ATR has the most predominant effect on enhancing recombinant protein productivity. The insights obtained from batch studies were used to investigate fed-batch processes, both during complete development of ATR and during suppression of ATR. During complete ATR-development, a 25-fold enhancement of volumetric productivity was achieved in fed-batch culture, due to a synergistic combination of increased glucose-feed rates and addition of complex-nutrients to the feed. A combination of these factors and ATR-suppression gave rise to nearly 60-fold increase in volumetric productivity in fed-batch culture over batch processes.

Production of scopularide A in submerged culture with Scopulariopsis brevicaulis.

BackgroundMarine organisms produce many novel compounds with useful biological activity, but are currently underexploited. Considerable research has been invested in the study of compounds from marine bacteria, and several groups have now recognised that marine fungi also produce an interesting range of compounds. During product discovery, these compounds are often produced only in non-agitated culture conditions, which are unfortunately not well suited for scaling up. A marine isolate of Scopulariopsis brevicaulis, strain LF580, produces the cyclodepsipeptide scopularide A, which has previously only been produced in non-agitated cultivation.ResultsScopulariopsis brevicaulis LF580 produced scopularide A when grown in batch and fed-batch submerged cultures. Scopularide A was extracted primarily from the biomass, with approximately 7% being extractable from the culture supernatant. By increasing the biomass density of the cultivations, we were able to increase the volumetric production of the cultures, but it was important to avoid nitrogen limitation. Specific production also increased with increasing biomass density, leading to improvements in volumetric production up to 29-fold, compared with previous, non-agitated cultivations. Cell densities up to 36 g L-1 were achieved in 1 to 10 L bioreactors. Production of scopularide A was optimised in complex medium, but was also possible in a completely defined medium.ConclusionsScopularide A production has been transferred from a non-agitated to a stirred tank bioreactor environment with an approximately 6-fold increase in specific and 29-fold increase in volumetric production. Production of scopularide A in stirred tank bioreactors demonstrates that marine fungal compounds can be suitable for scalable production, even with the native production organism.

Low Molecular Weight Protein Tyrosine Phosphatases Control Antibiotic Production in Streptomyces coelicolor A3(2)

Streptomyces coelicolor A3(2) possesses a low molecular weight protein tyrosine phosphatase (LMW-PTP), PtpA, that affects the production of undecylprodigionsin (RED) and actinorhodin (ACT). In this study we identified another LMW-PTP called sco3700. Tyrosine phosphatase activity of the purified Sco3700 was established using para-nitrophenyl phosphate and the tyrosine-phosphorylated protein PtkA from Bacillus subtilis as substrates. The optimum pH for the Sco3700 phosphatase activity was 6.8, and KM for pNPP was 14.3 mM compared to pH 6.0 and KM0.75 mM for PtpA. The potential of Sco3700 to participate, alongside PtpA, in the regulation of S. coelicolor antibiotic production was investigated. Hence, S. coelicolor A3(2) strains with ptpA and sco3700 overexpression were constructed and characterized for growth, RED and ACT production. We did observe an increase in volumetric productivity of ACT in the ptpA over expression strain. Furthermore, a significantly earlier onset of ACT production was observed when ptpA was over expressed. Sco3700 overexpression had a pleiotropic effect on the cell, and the strain exhibited lower productivities and final concentrations of antibiotics. We conclude that Sco3700 is indeed a tyrosine phosphatase, and it contributes to regulation of antibiotic production in S. coelicolor affecting the timing of onset of the antibiotic production.

Optimization of β-carotene production by a mutant of the lactose-positive yeast Rhodotorula acheniorum from whey ultrafiltrate

The present work investigated on carotenogenesis with high β-carotene content by a new isolated high-activity strain-producer Rhodotorula acheniorum mutant MRN in cheese whey ultrafiltrate. After a serial of UV, ethymethanesurfonate (EMS), and nitrosoguanidine (NTG) mutagenesis, a mutant named MRN of the red lactose-positive yeast strain R. acheniorum was obtained. Then, the effects of different growth medium factors on carotenoid production by this mutant at batch-scale level were identified and optimized by means of response surface methodology (RSM) in order to achieve high-level production of β-carotene. The optimum conditions required to achieve the highest level of β-carotene (262.12±1.01 mg/L) were determined as follows: whey ultrafiltrate (WU) lactose concentration 55 g/L, pH 5.85, ammonium sulfate concentration 3.5 g/L, temperature 23°C, and aeration rate 1.56 vvm. The medium optimization resulted in a 6.45-fold increase in volumetric production (262.12±1.01 mg/L) and a 4.62-fold increase in the cellular accumulation (10.69±0.19 mg/g) of β-carotene.

Lipase-Catalyzed Esterification of Ferulic Acid with Oleyl Alcohol in Ionic Liquid/Isooctane Binary Systems

Lipase-catalyzed synthesis of ferulic acid oleyl alcohol ester in an ionic liquid (IL)/isooctane system was investigated. Considerable bioconversion and volumetric productivity were achieved in inexpensive 1-hexyl-3-methylimidazolium hexafluorophosphate ([Hmim][PF(6)]) and 1-methyl-3-octylimidazolium hexafluorophosphate ([Omim][PF(6)]) mediated systems, and thus, the two types of ILs were selected for further optimization of variables. The results showed that, before reaching a maximum, the increase of ferulic acid concentration, temperature, or enzyme dosage led to an increase in volumetric productivity. Variations of the ratios of IL/isooctane and concentrations of oleyl alcohol also profoundly affected the volumetric productivity. To a higher extent, [Hmim][PF(6)]/isooctane and [Omim][PF(6)]/isooctane show similar reaction behaviors. Under the optimized reaction conditions (60 °C, 150 mg of Novozym 435 and 100 mg of molecular sieves), up to 48.50 mg/mL productivity of oleyl feruleate could be achieved for the [Hmim][PF(6)]/isooctane (0.5 mL/1.5 mL) system with a substrate concentration of ferulic acid of 0.08 mmol/mL and oleyl alcohol of 0.32 mmol; while an optimum volumetric productivity of 26.92 mg/mL was obtained for the [Omim][PF(6)]/ isooctane (0.5 mL/1.5 mL) system under a similar reaction condition other than the substrate concentrations of ferulic acid at 0.05 mmol/mL and oleyl alcohol at 0.20 mmol.

High productivity of human recombinant beta-interferon from a low-temperature perfusion culture

Recombinant human interferon-beta (β-IFN), used in the therapeutic treatment of multiple sclerosis (MS), can be produced on a large-scale from genetically engineered Chinese hamster ovary (CHO) cells. However, its hydrophobicity causes non-reversible, molecular aggregation in culture. The parameters affecting aggregation were determined to be concentration, culture residence time, temperature and glycosylation. Although the protein can be produced in Escherichia coli in a non-glycosylated form, the addition of glycans confers a reduced rate of aggregation as well as a 10-fold higher bioactivity. We report on the application of a low temperature perfusion culture designed to control the parameters that cause aggregation. In this three-phase culture system there is a transition to a low temperature (32 °C) in a batch mode prior to implementing perfusion at 1 volume/day using an acoustic cell separator. Perfusion at the low temperature resulted in a 3.5-fold increase in specific productivity and a 7-fold increase in volumetric productivity compared to the batch culture at 37 °C. The percentage aggregation of β-IFN was reduced from a maximum of 43% in batch culture to a minimum of 5% toward the end of the perfusion phase. The glycosylation profile of all samples showed predominantly sialylated biantennary fucosylated structures. The extent of sialylation, which is important for bioactivity, was enhanced significantly in the perfusion culture, compared to the batch culture.

Repeated-batch fermentation using flocculent hybrid, Saccharomyces cerevisiae CHFY0321 for efficient production of bioethanol

In this study, the repeated-batch fermentation of liquefied cassava medium using the flocculent hybrid Saccharomyces cerevisiae CHFY0321 was investigated for semicontinuous, high-throughput production of bioethanol. Cassava medium was selected due to the industrial requirement for a cheap starchy substrate. Fermentations were performed by simultaneous saccharification and fermentation (SSF) with a set of ten batches successfully completing a series within the repeated fermentation process. In addition, pH of the culture medium was not controlled to simplify ethanol production for future use in industry. Optimal recycling volume was found to be 5%. Volumetric productivity, final ethanol concentration, and ethanol yield were measured at 3.34 g l(-1) h(-1), 84.5 g l(-1), and 90.7%, respectively. Cell recycling (24.5 g DCW l(-1)) resulted in 1.8-fold decrease in fermentation time (24 h) and 1.8-fold increase in volumetric productivity compared with the ordinary batch fermentation. Therefore, repeated-batch SSF using flocculent CHFY0321 demonstrates the possibility of cost-effective bioethanol production by eliminating additional saccharification and inoculation steps.

Solvent‐impregnated resins as an in situ product recovery tool for phenol recovery from Pseudomonas putida S12TPL fermentations

The sustainable production of fine/bulk chemicals is often hampered by product toxicity and inhibition to the producing micro-organisms. Consequently, the product must be removed from the micro-organisms' environment. To achieve this, so-called solvent-impregnated resins (SIRs) as well as commercial resins have been added to a Pseudomonas putida S12TPL fermentation that produces phenol as a model compound from glucose. The SIRs contained an ionic liquid which extracts phenol effectively. It was observed that the addition of these particles resulted in an increased phenol production of more than a fourfold while the commercial resin (XAD-4) which is widely used in aromatic removal from aqueous phases, only gave a 2.5-fold increase in volumetric production.

Poly(3-hydroxybutyrate) synthesis from glycerol by a recombinant Escherichia coli arcA mutant in fed-batch microaerobic cultures

Poly(3-hydroxybutyrate) (PHB) synthesis was analyzed under microaerobic conditions in a recombinant Escherichia coli arcA mutant using glycerol as the main carbon source. The effect of several additives was assessed in a semi-synthetic medium by the 'one-factor-at-a-time' technique. Casein amino acids (CAS) concentration was an important factor influencing both growth and PHB accumulation. Three factors exerting a statistically significant influence on PHB synthesis were selected by using a Plackett-Burman screening design [glycerol, CAS, and initial cell dry weight (CDW) concentrations] and then optimized through a Box-Wilson design. Under such optimized conditions (22.02 g l(-1) glycerol, 1.78 g l(-1) CAS, and 1.83 g l(-1) inoculum) microaerobic batch cultures gave rise to 8.37 g l(-1) CDW and 3.52 g l(-1) PHB in 48 h (PHB content of 42%) in a benchtop bioreactor. Further improvements in microaerobic PHB accumulation were obtained in fed-batch cultures, in which glycerol was added to maintain its concentration above 5 g l(-1). After 60 h, CDW and PHB concentration reached 21.17 and 10.81 g l(-1), respectively, which results in a PHB content of 51%. Microaerobic fed-batch cultures allowed a 2.57-fold increase in volumetric productivity when compared with batch cultures.

High yield expression of recombinant pro-resilin: Lactose-induced fermentation in E. coli and facile purification

Resilin is an elastic protein with outstanding material properties: high resilience and a very high fatigue lifetime. We are interested in the production of resilin-like proteins which can be photo-chemically cross-linked to form rubbery biomaterials to be used in a variety of industrial and medicinal applications. A method has been developed for producing soluble recombinant proteins in small scale fermentation equipment using glycerol batch for initial growth and primary induction by IPTG at carbon source depletion, followed by new growth in lactose-induced culture. Recombinant rec1-resilin [1] has been over-expressed in the host strain Escherichia coli BL21(DE3)pLysS at a level of up to 300 mg/l, a greater than 20-fold increase in volumetric productivity, relative to that obtained from conventional IPTG induction in LB medium. The primary induction step before lactose induction in fresh medium resulted in a 2.5- to 3-fold increase of both volumetric productivity and cell specific yield compared to that without primary induction under the same conditions. This method is amenable and suitable for large scale production of soluble resilin-like proteins at a low operating cost. In addition, a simple ‘salt precipitation and heat purification’ method allowed rapid and efficient downstream processing of a large quantity of soluble recombinant resilin-like proteins. These methods will enable investigation of the structural and functional properties of resilin-like proteins, and the development of highly resilient biomaterials.

Effect of culture pH on erythropoietin production by Chinese hamster ovary cells grown in suspension at 32.5 and 37.0°C

To investigate the effect of culture pH in the range of 6.85-7.80 on cell growth and erythropoietin (EPO) production at 32.5 and 37.0 degrees C, serum-free suspension cultures of recombinant CHO cells (rCHO) were performed in a bioreactor with pH control. Lowering culture temperature from 37.0 to 32.5 degrees C suppressed cell growth, but cell viability remained high for a longer culture period. Regardless of culture temperature, the highest specific growth rate (mu) and maximum viable cell concentration were obtained at pH values of 7.00 and 7.20, respectively. Like mu, the specific consumption rates of glucose and glutamine decreased at 32.5 degrees C compared to 37.0 degrees C. In addition, they increased with increasing culture pH. Culture pH at 32.5 degrees C affected specific EPO productivity (q(EPO)) in a different fashion from that at 37 degrees C. At 37 degrees C, the q(EPO) was fairly constant in the pH range of 6.85-7.80, while at 32.5 degrees C, the q(EPO) was significantly influenced by culture pH. The highest q(EPO) was obtained at pH 7.00 and 32.5 degrees C, and its value was approximately 1.5-fold higher than that at pH 7.00 and 37.0 degrees C. The proportion of acidic EPO isoforms, which is a critical factor for high in vivo biological activity of EPO, was highest in the stationary phase of growth, regardless of culture temperature and pH. Although cell viability rapidly decreased in death phase at both 32.5 and 37.0 degrees C, the significant degradation of produced EPO, probably by the action of proteases released from lysed cells, was observed only at 37.0 degrees C. Taken together, through the optimization of culture temperature and pH, a 3-fold increase in maximum EPO concentration and a 1.4-fold increase in volumetric productivity were obtained at pH 7.00 and 32.5 degrees C when compared with those at 37.0 degrees C. These results demonstrate the importance of optimization of culture temperature and pH for enhancing EPO production in serum-free, suspension culture of rCHO cells.