PubMed Health⌕ Search

Biomedical subjects

J L Moreira

Publications and source records attributed to J L Moreira.

At least 19 recordsLinked to original sources
PubMed2005

Modelling and optimization of a recombinant BHK-21 cultivation process using hybrid grey-box systems.

In this work a model-based optimization study of fed-batch BHK-21 cultures expressing the human fusion glycoprotein IgG1-IL2 was performed. It was concluded that due to the complexity of the BHK metabolism it is rather difficult to develop a kinetic model with sufficient accuracy for optimization studies. Many kinetic expressions and a large number of parameters are involved resulting in a complex identification problem. For this reason, an alternative more cost-effective methodology based on hybrid grey-box models was adopted. Several model structures combining the a priori reliable first principles knowledge with black-box models were investigated using data from batch and fed-batch experiments. It has been reported in previous studies that the BHK metabolism exhibits modulation particularities when compared to other mammalian cell lines. It was concluded that these mechanisms were effectively captured by the hybrid model, this being of crucial importance for the successful optimization of the process operation. A method was proposed to monitor the risk of hybrid model unreliability and to constraint the optimization results to acceptable risk levels. From the optimization study it was concluded that the process productivity may be considerably increased if the glutamine and glucose concentrations are maintained at low levels during the growth phase and then glutamine feeding is increased.

Animals↗
PubMed2002

Process development of a recombinant antibody/interleukin-2 fusion protein expressed in protein-free medium by BHK cells.

The production, purification and stability of quality (in terms of integrity and glycosylation) of an antibody/interleukin-2 fusion protein with potential application in tumour-targeted therapy expressed in BHK21 cells are described. Consistency of the product throughout time was determined by analysis of glycosylation of the fusion protein using MALDI-TOF mass spectroscopy and HPAEC-PAD combined with product integrity studies by SDS-PAGE and Western blotting. These investigations showed consistent expression in terms of integrity and of three major oligosaccharide structures of the fusion protein after 62 generations. The data obtained at this stage indicated the suitability of the cell line for production purposes. Different approaches for the production of this protein were subsequently carried out. The relative productivity of the recombinant fusion protein and general performance of the cells in two different protein-free medium (PFM) culture systems, continuous chemostat and continuous perfusion using a Centritech centrifuge as a cell retention device, were studied. The results indicate that the chemostat culture resulted in more stable and controllable nutrient environment, which could indicate better product consistency, in accordance with what has been observed under serum-containing conditions, in relation to the perfusion culture. Finally, product obtained from the chemostat culture was analysed and purified. The purification process was optimised with an increase in the overall yield from 38 to 70% being obtained, a significant improvement with important consequences for the implementation of an industrial-scale culture system. In conclusion, it was possible to produce and purify the recombinant antibody/interleukin-2 fusion protein assuring the quality and stability of the product in terms of integrity and glycosylation. Therefore, a candidate production process was established.

Animals↗
PubMed2001

Strategies to modulate BHK cell proliferation by the regulation of IRF-1 expression.

Activation of the constitutively expressed interferon-regulatory-factor-1/estrogen receptor fusion protein (IRF-1-hER) in BHK cells was accomplished through the addition of estradiol to the culture medium, which enabled IRF-1 to gain its transcriptional activator function and inhibit cell growth. With the addition of 100 nM estradiol at the beginning of the exponential phase of a cell suspension culture, IRF-1 activation led to a rapid cell growth inhibition but also to a significant decrease in cell viability. To apply this concept in industry, a reduction of the time span of estradiol exposure is required. Cycles of estradiol addition and removal were performed in 2-l stirred tank bioreactors operated under perfusion, where an initial step addition of 100 nM estradiol was performed, followed, after 48-72 h, by a slow dilution with estradiol-free fresh medium (perfusion rate varying between 0.7 and 1.4 per day). Cell growth inhibition was successfully achieved for three consecutive cycles. Diluting the estradiol by perfusing medium without estradiol to concentrations lower than 10 nM led to cell growth and viability recovery independently of the perfusion rate used. These observations permitted the definition of operational strategies for regulated IRF-1 BHK cell growth by pulse estradiol addition, followed by a period of 48 h in the presence of estradiol and by fast perfusion to estradiol concentrations lower than 10 nM. Cell growth response to IRF-1 activation and following estradiol removal by perfusion was also evaluated with an IRF-1-hER regulated clone expressing constitutively Factor VII, where the time of estradiol exposure and perfusion rate were varied. This clone presented a stronger response to IRF-1 activation without an increase in Factor VII specific productivity after cell growth inhibition; this clearly indicates that the stationary phase obtained is clone dependent. This work proves that it is possible to modulate the IRF-1 effect for cell growth control by the manipulation of cycles of addition and removal of estradiol, potentially representing a new generation of culture procedures for controlled growth production purposes.

Animals↗
PubMed2000

Metabolic shifts do not influence the glycosylation patterns of a recombinant fusion protein expressed in BHK cells.

BHK-21 cells expressing a human IgG-IL2 fusion protein, with potential application in tumor-targeted therapy, were grown under different nutrient conditions in a continuous system for a time period of 80 days. At very low-glucose (< 0.5 mM) or glutamine (< 0. 2 mM) concentrations, a shift toward an energetically more efficient metabolism was observed. Cell-specific productivity was maintained under metabolically shifted growth conditions and at the same time an almost identical intracellular ATP content, obtained by in vivo (31)P NMR experiments, was observed. No significant differences in the oligosaccharide structures were detected from the IgG-IL2 fusion protein preparations obtained by growing cells under the different metabolic states. By using oligosaccharide mapping and MALDI/TOF-MS, only neutral diantennary oligosaccharides with or without core alpha1-6-linked fucose were detected that carried no, one or two beta1-4-linked galactose. Although the O-linked oligosaccharide structures that are present in the IL2 moiety of the protein were studied with less detail, the data obtained from the hydrazinolysis procedure point to the presence of the classical NeuAcalpha2-3Galbeta1-3GalNAc structure. Here, it is shown that under different defined cellular metabolic states, the quality of a recombinant product in terms of O- and N-linked oligosaccharides is stable, even after a prolonged cultivation period. Moreover, unaffected intracellular ATP levels under the different metabolic states were observed.

Animals↗
PubMed2000

Metabolically optimised BHK cell fed-batch cultures.

The aim of this work was the optimisation of a fed-batch culture by metabolic confinement of BHK21 cells producing an antibody/cytokine fusion protein with potential application in tumour-targeted therapy. Previous results showed that at very low nutrient concentrations, a metabolic shift towards more efficient metabolic pathways occurs. The application of those results in the optimisation of a fed-batch culture resulted in higher cell growth (0.020 vs. 0.016 h(-1)) and cell viability, higher maximum cell concentration (2.5 vs. 1.1x10(6) cell ml(-1)), longer culture span (17 versus nine days) and higher product titre (60% increase), in relation to batch culture. This was achieved by maintaining glucose at 0.3 mM and glutamine at 0.2 mM through the addition of a concentrated solution based on the estimations of future nutrient consumption and growth rates through off line measurements. The production of toxic metabolites such as lactate and ammonia was reduced, especially the lactate production, which was markedly decreased due to the metabolic confinement of the cells. In conclusion, it was possible to increase the final titre of the recombinant antibody/cytokine fusion protein by confining the metabolism of the cells to an energetically more efficient state.

Animals↗
PubMed1999

Proteolytic activity in infected and noninfected insect cells: degradation of HIV-1 Pr55gag particles.

In this work the proteolytic activity in the supernatant and inside insect cells in culture was evaluated for different multiplicities of infection (MOI) and times of infection (TOI). Several methods to detect proteolytic activity in insect cells were tested and that using fluorescein thiocyanite-casein as a substrate was chosen. It was observed that infection caused not only a reduction in the concentration of proteases by decreasing their synthesis but also an inhibition of the intracellular proteolytic activity by increasing the intracellular ATP level (measured by in vivo nuclear magnetic resonance, NMR). The maximum proteolytic activity in the supernatant was observed at 72 hpi except when the cells were infected in the late exponential growth phase or with very low MOI, yielding a nonsynchronous infection. The proteolytic degradation of Pr55gag particles was studied during culture and after harvest. In this particular case it was concluded that the supernatant should be stored at low temperature or quickly purified, since the degradation after 24 h is only 3% at 4 degrees C while at 27 degrees C this value rises to 23%. There is a complex relationship between MOI, TOI, proteolytic activity, and product titer and quality. Thus, the optimal conditions for each case will be a compromise between the final product titer, the desired product quality, and operational issues like process time and capacity, requiring proper integration between bioreaction and downstream processing.

Adenosine Triphosphate↗
PubMed1999

Metabolic shifts by nutrient manipulation in continuous cultures of BHK cells.

The present work aims at characterizing the regulatory mechanisms of metabolism and product formation of BHK cells producing a recombinant antibody/cytokine fusion protein. This work was carried out through the achievement of several steady-states in chemostat cultures, corresponding to different glucose and glutamine levels in the feed culture medium. Results obtained indicate that both glucose and glutamine consumptions show a Michaelis-Menten dependence on residual glucose and glutamine concentrations, respectively. Similar dependence was also observed for lactate and ammonia productions. K(Glc)(Glc) and K(Gln)(Gln) were estimated to be 0.4 and 0.15 mM, respectively, while q(max)(Glc) and q(max)(Gln) were estimated to be 1.8 and 0.55 nmol 10(-6)cells min(-1), respectively. At very low glucose concentrations, the glucose-to-lactate yield decreased markedly showing a metabolic shift towards lower lactate production; also, the glucose-to-cells yield was increased. At very low-glutamine concentrations, the glutamine-to-ammonia and glutamine-to-cells yields increased, showing a more efficient glutamine metabolism. Overall, amino acid consumption was increased under low glucose or glutamine concentrations. Metabolic-flux analysis confirmed the metabolic shifts by showing increases in the fluxes of the more energetically efficient pathways, at low-nutrient concentrations. No effect of glucose or glutamine concentrations on the cell-specific productivity was observed, even under metabolically shifted metabolism; therefore, it is possible to confine the cells to a more efficient metabolic state maintaining the productivity of the recombinant product of interest, and consequently, increasing final product titers by increasing cell concentration and culture length. This work is intended to be a model approach to characterize cell metabolism in an integrated way; it is highly valuable for the establishment of operating strategies in mammalian cell fermentations in which cell metabolism is to be confined to a desired state.

Amino Acids↗
PubMed1999

Metabolic responses to different glucose and glutamine levels in baby hamster kidney cell culture.

In this work, a BHK21 clone producing a recombinant antibody/cytokine fusion protein was used to study the dependence of cell metabolism on the glucose and glutamine levels in the culture medium. Results obtained indicate that both glucose and glutamine consumptions show a Michaelis-Menten dependence on glucose and glutamine concentrations respectively. A similar dependence is also observed for lactate and ammonia productions. The estimated value of the Michaelis constant for the dependence of lactate production on glucose (KLacGlc) was 1.4 +/- 0.1 mM and for the dependence of ammonia production on glutamine (KAmmGln) was 0.25 +/- 0.11 mM and 0.10 +/- 0.03 mM, at glucose concentrations of 0.28 mM and 5.6 mM respectively. At very low glucose concentrations, the glucose to lactate yield decreased markedly, showing a metabolic shift towards lower lactate production. This metabolic shift was also confirmed by the significant increase in the specific oxygen consumption rate also observed at low glucose concentrations. Although it was highly dependent on glucose concentration, the oxygen consumption also increased with the increase in glutamine concentration. At very low glutamine concentrations, the glutamine to ammonia yield increased, showing a more efficient glutamine metabolism.

Ammonia↗
PubMed1999

An integrated strategy for the process development of a recombinant antibody-cytokine fusion protein expressed in BHK cells.

Recombinant fusion proteins offer important new therapeutic approaches for the future. This report describes the use of three different genetic strategies (i.e. "mono-", "bi-" and "tri-cistronic" vectors) to achieve stable secretion from BHK cells of a glycosylated antibody-cytokine fusion protein designed for use in antitumour therapy. It describes selection of a robust and effective production cell line based on stability of secretion of the product, quality of mRNA and protein products and performance in in vitro bioassays for potency. The data obtained at this stage were utilised in the selection of a suitable candidate production cell line. The relative productivity and general performance of the cells in stirred tank and fixed bed culture systems indicated that a variety of cell culture technologies provided robust tools for production of a highly selected cell clone. Consistency of the product glycosylation was determined by analysis of released oligosaccharides using matrix-assisted laser desorption ionisation-time of flight mass spectrometry and high-performance anion exchange chromatography. These investigations showed consistent expression of three glycoforms of the fusion protein which varied in their relative proportions in different culture systems and at different time points in a fixed bed reactor with continuous perfusion. In conclusion, this study dealt with a range of important scientific and technical issues which are essential for regulatory approval and commercial success of a recombinant protein and elucidates some useful markers for process development for similar recombinant biologicals.

Animals↗
PubMed1998

Optimization of the production of virus-like particles in insect cells.

In this work the maximal operational hydrodynamic conditions (agitation and aeration rate) that cause no adverse effect in Sf-9 cells growth in SF900II serum-free medium were determined. Shear stresses higher than 1 N m-2 and aeration rates higher than 0.04 vvm affect cell growth and when these conditions increase to 1.5 N m-2 and 0.11 vvm, cell growth is completely inhibited with significant cell morphology changes and a strong decrease in viability. Although the pO2 did not show a significant effect upon cell growth in the range from 10 to 50%, cell infection and specific productivity were dramatically affected. The production was optimal at a pO2 of 25% with decreases higher than 50% being observed when the pO2 decreased to 10 or increased to 50%. The maximum product quality, i.e., the percentage of product in the form of high molecular weight particles, is not coincident with maximum product titer. Although the highest Pr55gag particle titer was obtained at 96 hours post infection (hpi) and at pO2 of 25%, the best product quality (defined by gel filtration chromatography and Western immunoblot) was obtained at 48 hpi, independently of the pO2 used. The effect of overcritical conditions upon productivity was also studied. As obtained for cell growth, cell infection is affected by shear stresses above 1 N m-2 and by aeration rates higher than 0.04 vvm, with decreases in Pr55gag particle titer higher than 70%, even when the overcritical values are still far from the limit at which cell death occurs. The results obtained and the optimization strategy used allowed the maximization of the oxygen supply without damaging the cells, with important consequences on the scale-up of a production process involving this insect cell/baculovirus expression system.

Animals↗
PubMed1997

Cell-dislodging methods under serum-free conditions.

In this work, a BHK21 clone producing a fusion protein consisting of a recombinant human IgG molecule with a cytokine tail, growing in a protein-free medium, was used to test several alternatives to avoid the use of serum for trypsin inactivation, currently used in cell dislodging. These included (1) trypsin inactivated with soybean trypsin inhibitor (STI); (2) cell dissociation solution instead of trypsin; (3) dispase instead of trypsin; (4) trypsin inactivated with fetal calf serum (positive control); (5) non-inactivated trypsin (negative control). Use of a centrifugation step was also tested for each alternative. Results indicate that the best method regarding cell growth, viability and adherent fraction is to use trypsin inactivated with STI followed by a centrifugation step. For all methods tested, the utilization of a centrifugation step always led to improved results. The optimal proportion for total trypsin inactivation is 1:1 trypsin (0.2% w/v) to STI (1 mg ml-1). equivalent to 2 mg trypsin to 1 mg STI. No toxic effect was observed for STI at the concentrations used. Long-term subculturing with this new, alternative dislodging method did not affect cell growth, viability and productivity.

Animals↗
PubMed1994

Studies of baby hamster kidney natural cell aggregation in suspended batch cultures.

Microcarrier cultures of animal cells of industrial relevance are known to shed aggregates into the suspension phase. For a BHK cell line, which is known to be prone to aggregate naturally, microcarrier and aggregate forms of culture are compared in spinner culture. In microcarrier cultures, it is shown that increasing initial microcarrier concentration yields decreasing concentration of smaller aggregates in suspension; roughly equivalent concentrations of total cells and single cells in suspension are obtained. In the absence of Cytodex 3, aggregate final size is hydrodynamically controlled in batch and semicontinuous suspension culture. Rate of agitation is the main variable controlling aggregate size in batch cultures. The range of agitation rates studied (20 to 70 rpm in 250 mL spinner flasks) produced aggregates with maximum sizes of 200 microns. Necrotic centers were not observed; this was confirmed by Trypan blue viability measurements after mechanical dissociation of aggregates and also by the constant productivity obtained from different aggregate sizes. Comparing aggregate and microcarrier culture conditions, it is shown that at 100 rpm maximum total cell concentration is larger in the absence of microcarriers; dead cell concentrations, most of which exist in suspension, are slightly larger in microcarrier culture. Total viable cell concentrations in aggregate, hydrodynamically controlled culture, are almost one order of magnitude higher than in microcarrier cultures. These results suggest that there might be advantages in using aggregate cultures under hydrodynamic control of aggregate size in lieu of microcarrier cultures for naturally aggregating cell lines.

Animals↗
PubMed1994

Expression of recombinant antibody and secreted alkaline phosphatase in mammalian cells. Influence of cell line and culture system upon production kinetics.

The growth and productivity of an Sp2/0 cell line, F3b10, expressing a recombinant antibody (rAb) and BHK21 cells expressing either the same rAb from the same plasmids (BHK.IgG) or secreted alkaline phosphatase (SEAP) (BHK.SEAP) were investigated. The F3b10 line was grown as a single cell suspension. The BHK lines were grown either as suspended natural aggregates or on Cytodex 3 microcarriers. The data for F3b10 showed that the cell-specific rAb production rate (QsrAb) increased in parallel with increases in the specific growth rate (mu). A similar result was obtained for suspended aggregate cultures of both recombinant BHK cell lines. In contrast, for microcarrier cultures of both BHK cell lines, Qsproduct increased as mu decreased. This report shows that the relationship between cell growth and Qsproduct for the cell lines and products studied is dependent upon the culture process. In systems where recombinant cells are growing as a single cell suspension or within a natural suspension aggregrate, Qsproduct increased with increases in mu. In such systems, the cells have a rounded morphology. When cells were grown on microcarriers. Qsproduct decreased as mu increased. Cells growing attached to a surface are flat and elongated. The observed differences in the relationship of Qsproduct to mu are correlated with changes in cell morphology. The relationship between Qsproduct and mu is also affected by the choice of cell line.

Alkaline Phosphatase↗
PubMed1994

Changes in animal cell natural aggregates in suspended batch cultures.

Some anchorage-dependent animal cells can form natural aggregates in stirred tanks. Baby hamster kidney (BHK) natural aggregates are described and characterized. Total cell concentration and viability could be obtained after aggregate mechanical dissociation, with negligible cell lysis and no change in cell membrane permeability. During a normal batch run, aggregates were formed immediately after inoculation, a few spherical aggregates increasing in size during the initial growth phase. At the end of the growth phase, an increase in aggregate concentration was observed, without a considerable increase in aggregate diameter. At the end of the batch run, 160 h after inoculation, aggregates disintegrated into smaller, non-spherical units, following a sharp viability decrease. Cell concentrations of 1.2 x 10(6) cells/ml were obtained, with 60% of the total cells being in aggregates; the cell concentration in aggregates achieved 5 x 10(8) cells/ml, with a porosity of 55%. Viability was consistently in the range 85-90%, both for aggregate and suspended cells.

Animals↗
PubMed1994

Repeated-batch cultures of baby hamster kidney cell aggregates in stirred vessels.

Natural aggregates of Baby Hamster Kidney cells were grown in stirred vessels operated as repeated-batch cultures during more than 600 hours. Different protocols were applied to passaging different fractions of the initial culture: single cells, large size distributed aggregates and large aggregates. When single cells or aggregates with the same size distribution found in culture are used as inoculum, it is possible to maintain semi-continuous cultures during more than 600 hours while keeping cell growth and viability. These results suggest that aggregate culture in large scale might be feasible, since a small scale culture can easily be used as inoculum for larger vessels without noticeable modification of the aggregate characteristics. However, when only the large aggregates are used as inoculum, it was shown that much lower cell concentrations are obtained, cell viability in aggregates dropping to less than 60%. Under this 'selection' procedure, aggregates maintain a constant size, larger than under batch experiments, up to approximately 400 hours; after this time, aggregate size increases to almost twice the size expected from batch cultures.

Alkaline Phosphatase↗