Growth and functional harvesting of human mesenchymal stromal cells cultured on a microcarrier-based system.

Human mesenchymal stromal cells (hMSCs) cells are attractive for applications in tissue engineering and cell therapy. Because of the low availability of hMSCs in tissues and the high doses of hMSCs necessary for infusion, scalable and cost-effective technologies for in vitro cell expansion are needed to produce MSCs while maintaining their functional, immunophenotypic and cytogenetic characteristics. Microcarrier-based culture systems are a good alternative to traditional systems for hMSC expansion. The aim of the present study was to develop a scalable bioprocess for the expansion of human bone marrow mesenchymal stromal cells (hBM-MSCs) on microcarriers to optimize growth and functional harvesting. In general, the results obtained demonstrated the feasibility of expanding hBM-MSCs using microcarrier technology. The maximum cell concentration (n = 5) was ~4.82 ± 1.18 × 10(5) cell mL(-1) at day 7, representing a 3.9-fold increase relative to the amount of inoculated cells. At the end of culture, 87.2% of the cells could be harvested (viability = 95%). Cell metabolism analysis revealed that there was no depletion of important nutrients such as glucose and glutamine during culture, and neither lactate nor ammonia byproducts were formed at inhibitory concentrations. The cells that were recovered after the expansion retained their immunophenotypic and functional characteristics. These results represent an important step toward the implementation of a GMP-compliant large-scale production system for hMSCs for cellular therapy.

Effect of hypothermic temperatures on production of rabies virus glycoprotein by recombinant Drosophila melanogaster S2 cells cultured in suspension.

Aiming at maximizing the production of transmembrane rabies virus glycoprotein (rRVGP), the influence of hypothermic temperature on a recombinant Drosophila melanogaster S2 cell culture in Sf-900II medium was investigated. Cell growth and rRVGP production were assessed at 4 culture temperatures in Schott flasks: 16, 20, 24 and 28 °C. The maximum specific growth rates µ(max) were, respectively: 0.009, 0.019, 0.038 and 0.035 h(-1), while the maximum rRVGP levels C(max)(rRVGP) were: 0.075, 2.973, 0.480 and 1.404 mg L(-1). The best production temperature (20 °C) was then tested in a bioreactor with control of pH and dissolved oxygen in batch and fed-batch modes. In the batch culture, µ(max) and C(max)(rRVGP) were 0.060 h(-1) and 0.149 mg L(-1) at 28 °C and 0.026 h(-1) and 0.354 mg L(-1) at 20 °C, respectively. One batch-culture experiment was carried out with adaptation of the cells by the temperature falling in steps from 20 °C to 16 °C, so that µ(max) fell from 0.023 to 0.013 h(-1), while C(max)(rRVGP) was improved to 0.567 mg L(-1). In the fed-batch mode at 20 °C, µ(max) was 0.025 h(-1) and C(max)(rRVGP) was 1.155 mg L(-1). Taken together, these results indicate that the best strategy for optimized rRVGP production is the culture at hypothermic temperature of 20 °C, when µ(max) is kept low and with feeding of limitant aminoacids.

Drosophila melanogaster S2 cells for expression of heterologous genes: From gene cloning to bioprocess development.

In the present review we discuss strategies that have been used for heterologous gene expression in Drosophila melanogaster Schneider 2 (S2) cells using plasmid vectors. Since the growth of S2 cells is not dependent on anchorage to solid substrates, these cells can be easily cultured in suspension in large volumes. The factors that most affect the growth and gene expression of S2 cells, namely cell line, cell passage, inoculum concentration, culture medium, temperature, dissolved oxygen concentration, pH, hydrodynamic forces and toxic metabolites, are discussed by comparison with other insect and mammalian cells. Gene expression, cell metabolism, culture medium formulation and parameters involved in cellular respiration are particularly emphasized. The experience of the authors with the successful expression of a biologically functional protein, the rabies virus glycoprotein (RVGP), by recombinant S2 cells is presented in the topics covered.

Nomenclature and guideline to express the amount of a membrane protein synthesized in animal cells in view of bioprocess optimization and production monitoring.

Studies of a bioprocess optimization and monitoring for protein synthesis in animal cells face a challenge on how to express in quantitative terms the system performance. It is possible to have a panel of calculated variables that fits more or less appropriately the intended goal. Each mathematical expression approach translates different quantitative aspects. We can basically separate them into two categories: those used for the evaluation of cell physiology in terms of product synthesis, which can be for bioprocess improvement or optimization, and those used for production unit sizing and for bioprocess operation. With these perspectives and based on our own data of kinetic S2 cells growth and metabolism, as well as on their synthesis of the transmembrane recombinant rabies virus glycoprotein, here indicated as P, we show and discuss the main characteristics of calculated variables and their recommended use. Mainly applied to a bioprocess improvement/optimization and that mainly used for operation definition and to design the production unit, we expect these definitions/recommendations would improve the quality of data produced in this field and lead to more standardized procedures. In turn, it would allow a better and easier comprehension of scientific and technological communications for specialized readers.

Enhanced production of recombinant rabies virus glycoprotein (rRVGP) by Drosophila melanogaster S2 cells through control of culture conditions.

Culture conditions that affect product quality are important to the successful operation and optimization of recombinant protein production. The objective of this study was to optimize culture conditions for growth of recombinant Drosophila melanogaster S2 cells (S2AcRVGP) in order to enhance the production of rRVGP. The addition of DMSO and glycerol to the medium and growth at a reduced temperature (22 degrees C) were the culture condition variations selected to be tested. Experimental cultures were first performed in serum-free Sf900 II medium in 250 ml Schott flasks. The most promising conditions identified in these experiments were also tested on a higher scale in a 3l bioreactor. In the Schott flasks experiments, all the changes in culture conditions resulted in an increase of rRVGP production. The protein concentration was 3.6-fold higher with addition of 1% DMSO and 1% glycerol and 9.3-fold higher when the cells were cultured at 22 degrees C instead of the standard 28 degrees C. The maximum concentration of rRVGP reached was 591 mug l(-1). In bioreactor experiments, with control of pH at 6.20 and DO at 50%, the reduced culture temperature (22 degrees C) was the strategy that promoted the highest glycoprotein production, 928 mug l(-1).

Characterization of growth and metabolism of Drosophila melanogaster cells transfected with the rabies-virus glycoprotein gene.

In the present study, the growth and key metabolic features of a gene-transfected Drosophila melanogaster (fruitfly) S2 (Schneider 2) cell population (S2AcRVGP cells), cultured in Sf900-II medium, have been evaluated to provide substantial support for the development of a bioprocess to produce RVGP (rabies-virus glycoprotein). Experimental cultures were grown both in a 100 ml Schott flask incubated in a shaker at 28 degrees C and 100 rev./min and in a 3 litre stirred-tank bioreactor at 28 degrees C, with increasing agitation. In small-scale culture, S2AcRVGP cells reached a maximum cell concentration of 1.13 x 10(7) cell/ml, presented a mu(max) (maximum specific growth rate) of 0.037 h(-1) and the growth was limited by oxygen deprivation. An early and remarkably long stationary phase was observed under hypoxia. Cell cultures grown in the bioreactor without oxygen limitation exhibited a maximum cell concentration of 2.2 x 10(7) cells/ml and mu(max) values as high as 0.048 h(-1). The main substrate consumed in order to reach such a high growth rate was the amino acid proline, which seems to play an important role as a source of metabolic energy in the culture of S2AcRVGP cells. Under conditions of hypoxia, the cells were able to survive for 15 h without apparent damage, recovering their previous metabolic activity.

Evaluating kinetic and physiological features of rCHO-K1 cells cultured on microcarriers for production of a recombinant metalloprotease/disintegrin

We present kinetic and physiological data regarding the culturing of rCHO-K1 cells on various microcarriers, to evaluate the potential of this culture strategy for mass production of these cells and expression of a recombinant disintegrin. Cultures were performed in 500 mL spinner flasks in DMEM culture medium with 10 percent v/v fetal calf serum, gently shaken at 37 C, pH 7.4, in a 10 percent v/v CO2 atmosphere. The following values were obtained, respectively, for the adhesion time-constant Ka (h) and specific growth rate micron max (d-1) on each microcarrier: Cytodex 1 (0.91, 0.45), Cultispher S (0.28, 0.34), Immobasil FS (0.85, 0.52) and Pronectin F (5.12, 0.67). Metabolic characteristics showed some variation among the cultures with the four microcarriers, the most significant being the higher production of ammonia with microcarriers coated with adhesive molecules (Cultispher S and Pronectin F) relative to the uncoated carriers (Cytodex 1 and Immobasil FS). Experiments where the DMEM medium was gradually replaced by the serum-free medium (CHO-SFM-II) revealed important advantages over media containing serum, not only for assay purposes, but also for purification of the disintegrin. Altogether these results demonstrate that cultures on microcarriers, especially on Pronectin F, show good potential for larger scale cultures of rCHO-K1 cell.

Evaluation of the performance of a novel ceramic membrane bioreactor using the fungus Penicillium chrysogenum

The fungus Penicillium chrysogenum IFO-8644 was grown in a new type of ceramic membrane bioreactor operating with synthetic and complex germination medium at 27§C and pH7.0, using membranes with average pore diameters of 2.28 mm and effective area of 26.5 cm². Tests with different age inocula, an important factor in the development of the microorganisms, were performed. The best results were obtained using fresh inocula. Another extremely important factor to be considered in the desing of the bioreactor was the available membrane area for the growth of the fungus. As to the metabolism, sucrose was confirmed as the best source of carbon and energy since glucose had a repressive effect on the antibiotic production. A mathematical model, based on Monod growth kinetics for cell inhibition, enabled a reliable representation of the behavior of the bioreactor. Analysis of the experimental and simulated results showed that the bioprecess is viable in the novel bioreactor and that this bioreactor presents very promising potentials for large scale use.