Performance study of perfusion cultures for the production of single-chain urokinase-type plasminogen activator (scu-PA) in a 2.5 l spin-filter bioreactor

A perfusion-control strategy based on cellular consumption rates of oxygen and glucose was established for the production of single-chain urokinase-type plasminogen activator (scu-PA). Employing this strategy, the influences of microcarrier types and the culture media on culture performances were evaluated. In the control perfusion culture, which used a solid microcarrier and a 1% fetal bovine serum (FBS) medium, viable cell density reached 3.1?×?10⁷?cells?ml^?1. However, formation of large, heterogeneous aggregates (500–1,000?μm) resulted in a gradual decrease in viable cell density to less than 1.0?×?10⁷?cells?ml^?1. Accordingly, declines in the production of urokinase-type plasminogen activator (u-PA) and in the scu-PA portion of u-PA were observed. In the serum-free media, cell growth and u-PA production were suppressed 2–3?times, but were significantly enhanced when a porous microcarrier, Cultispheer G, was used. The cell-growth profile showed a continuous increase in cell density, reaching 5.1?×?10⁷?cells?ml^?1, and the production of u-PA remained stable throughout the culture (1586?±?247?IU?ml^?1). The values of all the parameters associated with cell growth and u-PA production were fairly comparable to or even higher than those in the control culture. Moreover, a 13% higher scu-PA portion of u-PA was observed in the serum-free culture, regardless of the microcarrier type, compared with scu-PA portion of u-PA in the control culture.     

Adaptation of hybridoma cells to higher ammonia concentration

Using two mouse-mouse hybridoma cell lines, the response to ammonia step and serial changes was investigated in batch and continuous cultures with serum-free medium. The inhibitory effect of ammonia on cell growth depended on the cultivation mode, and differed markedly between cell lines. The cell line, 4C10B6 producing IgG monoclonal antibody against Pseudomonas, showed a high adaptation ability to ammonia. The 4C10B6 cells could grow under ammonia concentration as high as 21 mmol/l NH₄Cl with a viability of 80% in the continuous culture with serial increase in ammonia concentration. Whereas, in the batch culture with ammonia step change the cell growth completely ceased at 12 mmol/l NH₄Cl. The other cell line, TO-405 producing IgG monoclonal antibody against hepatitis B surface antigen, could not adapt to ammonia, and the cell growth did not occur at 9 mmol/l NH₄Cl even under the ammonia serial change.List of symbols D_Feed d^-1 Dilution rate of fresh feed medium (=F_o/V) - D_Out d^-1 Dilution rate of cell suspension (=F₁/V) - F₁ ml·d^-1 Volumetric discharge rate of cell suspension - F₀ ml·d^-1 Volumetric flow rate of fresh feed medium - k_D h^-1 Specific death rate - P mmol·l^-1 Product concentration - S mmol·l^-1 Substrate concentration in culture broth - S₀ mmol·l^-1 Substrate concentration in feed medium - t d Cultivation time - V ml Working volume of reactor - X₀ cells·ml^-1 Total cell density - X_V cells·ml^-1 Viable cell density - Y_P/S mmol·mmol^-1 Yield of product from substrate - Y_X/S cells·mmol^-1 Yield of cells from substrate - mmol·cell^-1·h^-1 Specific production rate - h^-1 Specific growth rate - mmol·cell^-1·h^-1 Specific consumption rate of substrate     

Characterization of Vero cell growth and death in bioreactor with serum-containing and serum-free media

The density of viable cells in a culture results from a balance between cell proliferation and cell death. The aim of this study was to characterize and compare these two phenomena in Vero cell cultures in one serum containing medium (ScA) and one serum free medium (SfB) in bioreactors. Cell growth was evaluated by cell counting(after crystal violet staining) and cell cycle analysis. Necrosis and apoptosis were characterized and quantified by measuring the release of LDH, trypan blue exclusion,annex in V-FITC/PI staining and TUNEL assay. ScA supported a higher maximal viable-cell density(2.3 × 10⁶ vs. 1.8 × 10⁶ cells ml^-1). However, cell cycle analysis showed that cell division was more active in SfB than in ScA. LDH release in the supernatant increased much earlier in SfB than in ScA (one vs. five days), but trypan blue counts showed no apparent difference in the viability of the cultures. Apoptosis, evidenced by annexin V-FITC/PI staining, could be detected in the population of suspension cells detached from microcarriers, but not among adherent cells; positivity of the TUNEL assay occurred later than that of the annexin V-FITC/PI staining. Our data indicate that the lower cell yield in SfB,compared with that in ScA, results from a higher cell death rate. Apparently, cells die from apoptosis followed by secondary necrosis. This revised version was published online in July 2006 with corrections to the Cover Date.     

Production of a membrane-bound proteins,the human gamma-glutamyl transferase,by CHO cells cultivated on microcarriers,in aggregates and in suspension

Recombinant Chinese Hamster Ovary (CHO) cells, engineered for the production of human gamma-glutamyl transferase (GGT), have been grown on Cytodex 1 microcarriers, as aggregates, or as single cells in suspension after adaptation. GGT is a membrane bound enzyme which was not secreted during the culture period. The maximal enzyme activity was found to be directly related to the achieved maximal cell density. Culture of CHO on microcarriers yielded the fastest growth, with a specific growth rate of 0.04 h^–1, the highest cell density (near 1.3×10⁶ cells ml^–1), and the highest enzyme activity around 300 mU ml^–1, which corresponded to a specific cellular level of 20 mU 10^–5 cells. GGT could also be produced by growing CHO cells in suspension as single cells or as aggregates. Under these conditions, however, the specific CHO growth rate was significantly slower and the GGT level per cell was divided by a factor 6. Growing CHO cells without microcarriers also resulted in differences in cell metabolism, with a higher conversion yield of glutamine into ammonia, and a higher cell lysis. The catalytic kinetic constants of the enzyme were found identical for the three culture systems.     

多孔微载体无血清培养rCHO细胞生产u-PA

在30L搅拌式反应器中无血清培养分泌尿激酶型纤溶酶原激活剂(u-PA)的DNA重组CHO细胞,定期部分更换Cytopore多孔微载体,使生长在多孔微载体中的细胞不断更新繁殖,解决大规模细胞培养中的细胞凋亡问题。在91d连接换液培养过程中,细胞密度可维持在(1.3～2.6)×107／mL,活细胞比率维持在90％以上。在7.5L搅拌罐中培养细胞,利用外部周期性压力振荡刺激并结合载体更新技术,可减轻密度效应对细胞生长和表达的影响,在一定程度上提高细胞在高密度培养条件下的表达水平。在67d连续换液培养中,细胞最高密度为2.64×107／mL,活细胞比率维持在95％以上。与稳压操作相比,利用周期变压刺激技术可提高产量10％～20％,且可降低葡萄糖厌氧代谢生成乳酸的转化率,利用4步纯化工艺,从含u-PA约135g的2100L上清中获得约80gu-PA(单链比例约为90％)。     

Adaptation of cholesterol-requiring NS0 mouse myeloma cells to high density growth in a fully defined protein-free and cholesterol-free culture medium

NS0 has been used as a fusion partner for the production of hybridomas and has more recently been engineered to produce recombinant protein. A protein-free culture medium, designated W38 medium, has previously been developed which supported high density growth of rat myeloma and hybridoma cell lines. NS0 cells failed to grow in W38 medium and in a number of protein-free culture media which support the growth of other myeloma cell lines. NS0 cells are derived from the NS-1 cell line, which is known to require exogencus cholesterol. It was found that NS0 cells grew in W38 medium supplemented with phosphatidylcholine, cholesterol, and albumin and that NS0 were auxotrophic for cholesterol. Protein-free growth of NS0 cells was achieved by using -cyclodextrin to replace albumin as a lipid carrier. The maximal cell density reached in this protein-free medium was in excess of 1.5×10⁶ cell ml^–1. The lipid supplements in the medium precipitated after a few days storage at +4°C. In order to overcome this problem a protocol was developed which allowed NS0 cells to be adapted to cholesterol-independent growth in W38 medium. NS0.CF (cholesterol-independent NS0 cells) were cultured continuously in W38 medium for several months. In shake flask culture a cell density of 2.4×10⁶ cells ml^–1 was achieved in W38 medium compared with 1.41×10⁶ cells ml^–1 in RPMI 1640 medium containing 10% foetal bovine serum. NS0.CF cells readily grew in a 1 litre stirred bioreactor using W38 medium supplemented with Pluronic F68 reaching a density of 3.24×10⁶ cells ml^–1. NS0.CF were cloned protein-free by limiting dilution in W38 medium, giving colonies in wells that were seeded at an average density of 0.32 cells per 200 l. This study has demonstrated for the first time the growth of a cholesterol-requiring mouse myeloma cell line in a completely defined protein-free medium and its subsequent adaptation to cholesterol-independence.Abbreviations BSA bovine serum albumin - C cholesterol - CD cyclodextrin - F68 Pluronic F68 - GS glutamine synthetase - P phosphatidylcholine - PC-FBS phosphatidylcholine, cholesterol and foetal bovine serum - RPMI RPMI 1640 medium - MSX methionine sulphoximine     

Growth hormone stimulates hepatic lipid mobilization in rainbow trout,Oncorhynchus mykiss

Rainbow trout were used to characterize the direct influence of growth hormone on hepatic lipid mobilization in vitro. Liver was removed from fish fasted 72 h, sliced into 1-mm³ pieces and incubated in Hanks' medium containing ovine or salmon growth hormone (0.28 ng·ml^-1–28 g·ml^-1). Lipid mobilization, resulting from triacylglycerol hydrolysis, was evaluated by fatty acid and glycerol release into culture medium. Control rates of fatty acid release and glycerol release were 0.95±0.16 (mean ± SE) and 0.88±0.28 mol·l^-1·mg fresh weight, respectively. Both ovine growth hormone (28 ng·ml^-1) and salmon growth hormone (28 ng·ml^-1) stimulated fatty acid release into culture medium, increasing rates by 112% and 97%, respectively, during the course of a 24-h incubation. Glycerol release was similarly augmented by growth hormone treatment. Growth hormone-stimulated metabolite release became evident within 12 h and persisted for up to 72 h. The presence of amino acids in the culture medium potentiated the lipolytic action of growth hormone. Ovine growth hormone (28 ng·ml^-1) in the presence of amino acids stimulated a 53% increase in fatty acid, and a 108% increase in glycerol, release over rates observed in the absence of amino acids. Salmon growth hormone (28 ng·ml^-1) in the presence of amino acids stimulated a 53% increase in fatty acid, and a 44% increase in glycerol, release over rates observed in the absence of amino acids. Ovine growth hormone (28 ng·ml^-1) also stimulated gluconeogenesis, as indicated by a 75% increase in phosphoenolpyruvate carboxykinase activity in liver pieces incubated in the presence of amino acids. These results indicate that growth hormone directly stimulates lipid breakdown in the liver of trout and that amino acids potentiate growth hormone-stimulated lipolysis.Abbreviations AA amino acid(s) - dGDP deoxy-guanosine diphosphate - ED ₅₀ 50% effective dose - FA fatty acid(s) - fw fesh weight - GH growth hormone - Hepes 4-(2-hydroxyethyl)-1-piperazineethanesulphonic acid - MS-222 tricaine methanesulfonate - MEM minimum essential medium - oGH ovine growth hormone - PEPCK phosphoenolpyruvate carboxykinase - PK_c protein kinase C - rpm revolutions per minute - sGH salmon growth hormone - TG triacylglycerol - w/v weight per volume This paper was presented in abstract form at the Annual Meeting of the American Society of Zoologists, Dec. 26–30, 1991, Atlanta, GA     

Development of a serum-free culture medium for the large scale production of recombinant protein from a Chinese hamster ovary cell line

A serum-free medium, WCM5, has been developed for the large scale propagation of CHO (Chinese hamster ovary) cells which express recombinant protein using dihydrofolate reductase as a selectable marker. WCM5 was prepared by supplementing Iscoves medium without lecithin, albumin or transferrin with a number of components which were shown to benefit growth. WCM5 medium contained 5 mg l^–1 human recombinant insulin (Nucellin) but was otherwise protein-free. CHO 3D11^* cells which had been engineered to express a humanised antibody, CAMPATH^*-1H, were routinely grown using serum-containing medium. From a seeding density of 10⁵ cells ml^–1, cells grown in static culture with serum reached a maximal cell density of 6.5×10⁵ cells ml^–1 after 6 days in culture and produced a maximal antibody concentration of 69 mg l^–1 after 11 days in culture. CHO 3D11^* cells grown with serum were washed in serum-free medium then cultured in WCM5 medium. Following a period of adaptation the cell growth and product yield was superior to that achieved with serum-containing medium. CHO cells producing CAMPATH-1H grown in an 8000 l stirred bioreactor seeded with 2×10⁵ cells ml^–1 reached a maximal viable cell density of 2.16×10⁶ cells ml^–1 after 108 h in culture and a maximal antibody concentration of 131.1 mg l^–1 after 122 h in culture.Abbreviations CHO Chinese hamster ovary - dhfr dihydrofolate reductase - dhfr dihydrofolate reductase deficient - MTX methotrexate - H hypoxanthine - T thymidine - T/V trypsin versene - F12 Hams F12 medium - NEAA non essential amino acids     

Nutritional requirements of protoplast-derived,haploid tobacco cells grown at low cell densities in liquid medium

Preliminary attempts to define a completely synthetic medium able to support divisions of haploid tobacco mesophyll protoplasts at low initial densities have failed. High protoplast concentrations together with large amounts of naphtaleneacetic acid in the medium (3 mg l^-1 NAA) were required for maximal induction of protoplast division. However, cell suspensions derived from haploid protoplasts after four days of preculture at high initial cell densities could be diluted to densities as low as 1–4 cells ml^-1, provided the concentration of NAA in the medium was lowered to below 0.3 mg l^-1. The optimal NAA supply for low cell density growth was affected by the nature of the nitrogen source.A simple minimal medium which supports the growth of these haploid cells with a plating efficiency of 30–40%, independent of the cell density in the range of 1–4 to 3·10⁴ cells ml^-1, has been established. In this medium inositol was the only vitamin stringently required for growth.Growth of cells at low densities was also possible in a medium initially containing 3 mg l^-1 NAA, provided it was conditioned by the growth of protoplasts at high densities. Preliminary experiments with [¹⁴C]NAA showed that the amount of free NAA remaining in the medium after preincubation at high densities was drastically reduced. Simultaneously, NAA conjugates accumulated in the medium. The implications of these results are discussed.Abbreviations BA 6-benzyladenine - EDTA ethylene diaminetetraacetic acid - NAA naphtaleneacetic acid     

The culture of rat myeloma and rat hybridoma cells in a protein-free medium

Y0 is a rat x rat hybridoma cell line, which does not secrete immunoglobulin, produced using a fusion partner derived from the Y3 (Y3,Ag.1.2.3) rat myoloma cell line. Y0 and Y3 have both been widely used as fusion partners in the production of rat x rat hybridomas. Y0 has also been used in recombinant gene technology. Y0 cells grown in shake flask culture, using RPMI 1640 medium with 4mM l-glutamine and 5% foetal bovine serum, reached a maximal cell density of 1.5×10⁶ cells ml^–1 with 86% viability. Y0 cells which has been adapted to grow in ABC protein-free medium reached a maximal density, in shake flask culture, of 8.75×10⁵ cells ml^–1 with 79% viability. An improved protein-free medium, designated W38 medium, was developed. In shake flask culture, W38 medium supported Y0 cell growth to a density of 2.02×10⁶ cells ml^–1 with 96% viability. Two Y3 hybridomas, YID 13.9.4 cells and SAM 618 cells were adapted to growth in W38 medium. For both hybridomas, cell growth and product yield in shake flask culture using W38 medium was superior to that obtained with serum-containing RPMI 1640 medium.Abbreviations F12 Hams F12 medium - DMEM Dulbeccos medium - RPMI RPMI 1640 medium - FBS foetal bovine serum     

A novel scale-up method for mammalian cell culture in packed-bed bioreactor

A novel method for the scale-up culture of Chinese hamster ovary (CHO) cells in a packed-bed bioreactor is developed wherein microcarriers, attached with CHO cells in a microcarrier culture system, are inoculated directly into the packed-bed bioreactor. Cells continue to grow after inoculation and the maximum cell density reaches about 2×10⁷ cells ml^–1. The method provides a new technique for the scale-up of a packed-bed culture while decreasing the labour cost and ensuring the safety of operation.     

Division and growth of mesophyll cells isolated from Psoralea bituminosa leaves

Mesophyll cells have been isolated from Psoralea bituminosa plant by gentle homogenization in a liquid nutrient medium. Between 60 and 70% of the cells can be isolated from leaves using this method, of which 50 to 60% can be recovered morphologically intact. Under light the separated cells have rates of oxygen evolution under light of 3500 μl O₂ mg^?1 chlorophyll h^?1 (measured with a Clark-type electrode). During growth, this rate decreases rapidly, as does cell pigments (chlorophylls and carotenoids). As a first step in obtaining a photoautotrophic cell suspension, growth factors affecting cell division in free sugar medium were investigated. The starting culture contained between 1 and 2 × 10⁶ cells ml^?1. The best increase in cell number was obtained on a medium composed of Joshi and Ball's elements and vitamins and containing 1 mg l^?1 of naphthalene acetic acid, 0.1 mg l^?1 of benzylaminopurine and the grinding juice. The optimum culture pH was between 5 and 5.3.     

A novel animal-component-free medium for rabies virus production in Vero cells grown on Cytodex 1 microcarriers in a stirred bioreactor

Vero cells growth and rabies production in IPT-AF medium, a property animal-component-free medium are described in this work. Kinetics of cell growth and rabies virus (strain LP 2061) production were first conducted in spinner flasks. Over eight independent experiments, Vero cell growth in IPT-AF medium, on 2 g/l Cytodex 1 was consistent. An average Cd (cell division number) of 3.3 ± 0.4 and a specific growth rate μ of 0.017 ± 0.006 h⁻¹ were achieved. Such performances were comparable to those obtained in serum-containing medium (MEM + 10% FCS). Rabies virus production on Vero cells in IPT-AF medium was also optimised in spinner flasks. The effects of multiplicity of infection (MOI), regulation of glucose level at 1 g/l and cell washing step, were investigated. The highest virus titer was achieved when the cells were infected at an MOI of 0.1; this level was equal to 10⁷ FFU/ml. The step of medium exchange before cell infection can be omitted; nevertheless in this case glucose level should be maintained at 1 g/l to avoid a decrease of specific virus productivity. Process optimisation in a 2-l stirred bioreactor pointed out that the aeration mode was the prominent parameter that affected cell growth in IPT-AF medium and on Cytodex 1 microcarriers. An acceptable level of cell density (cell density level of 1.5 × 10⁶ cells/ml) was achieved when cells were grown in batch mode and using headspace aeration. Nevertheless, this aeration mode is not optimal for large-scale culture. The addition of Pluronic F68 at 0.1% at 24 h post inoculation as well as the switch from surface aeration mode to the sparged mode, 2 days after the start of the culture, had markedly improved cell growth performance. A cell density level of 5.5 × 10⁶ cells/ml was reached when cells were grown in a 2-l bioreactor, on 3 g/l Cytodex 1 in IPT-AF medium and using the recirculation culture mode. Cell infection at an MOI of 0.1 and using perfused culture, resulted in a maximal virus titer of 3.5 × 10⁷ FFU/ml. The activity of the pooled inactivated rabies virus harvests showed a protective activity that meets WHO requirements.     

Serum-free production of a chimeric E-selectin-IgG protein from 1 to 100 l scale: Repeated batch cultivation versus continuous spin filter perfusion

On inflamed endothelium the cell surface protein E-selectin isexpressed which supports the initial process of attachment –capturing and rolling of leukocytes. A recombinant CHO cell linesecreting a soluble E-selectin-IgG chimera was cultivated competitively under serum free conditions in three different bioreactor systems: a 1 l Super-Spinner, a 2 l stirred tank bioreactor equipped with a spinfilter, and a 100 l stirred tankbioreactor. In the smallest system 25.4 mg E-selectin-IgG wereproduced in 62 days using a repeated batch process whileachieving a maximal viable cell density of 3.7 × 10⁶ cells ml^-1. Using continuous perfusion mode a total amount of35.2 mg were produced with a maximal viable cell density of1.65 × 10⁷ cells ml^-1 in the 2 l bioreactor within 29 days. Large scale cultivation in a 100 l stirred tankbioreactor yielded 105.6 mg in three batches with a maximal viable cell density of 9.7 × 10⁵ cells ml^-1 within 15 days. After removal of the cells by continuous centrifugation and a depth filter clearance step, the supernatants were concentrated via ultra filtration. Purificationwas performed by affinity chromatography with rProtein A. Integrity of the E-selectin-IgG protein was checked with SDS PAGE. Its activity was verified in a cellular adhesion assay performed with HL-60 cells and a recombinant CHO cell line expressing membrane-anchored E-selectin constitutively, and E-selectin expressing HUVECs, respectively. Soluble E-selectin-IgG was used to block adhesion to these cell layerscompetitively. A concentation of 18.8 and 37.5 g ml^-1was sufficient to reduce the amount of adhering HL-60 cells to 50% on CHO and HUVEC layers, respectively.     

Screening Wheat Genotypes for High Callus Induction and Regeneration Capability from Immature Embryo Cultures

Selecting the explant genotypes is crucial step in in vitro culture and Agrobacterium-mediated transformation system due to its host range specificity. Immature embryos of five winter and three spring wheat (Triticum aestivum L) cultivars were evaluated for tissue culture response in three callus initiation media. MS medium containing 2,4-0 (2 mg ml^-1) plus B5 vitamins (MSB5), MS medium containing 2,4-0 (1 mg ml^-1) with no vitamins (MS1GC) or MS medium containing picloram (2.2 mg ml^-1) and 2,4-0 (0.5 mg ml^-1) plus MS vitamins (CM4C) were used for callus initiation. Percentage of callus induction varied widely with the genotype and initiation medium used, with values ranging from 5.7% to 100%. Embryogenic capacity of genotypes was evaluated by number of somatic embryos formed from cultured immature embryos. Bob White (spring) and NE92458 (winter) were equal and most embryogenic; Pronghorn and 2137 (both winter) were the poorest. CM4C medium was found to be the best medium for initiating embryogenic callus among three culture media tested. A standard regeneration procedure was used. The genotypes with the highest regeneration efficiencies were Bob White, Fielder and NE92458, (1.8, 1.4 and 1.6 plantslexplant, respectively).     

Ex vivo expansion of bone marrow mesenchymal stem cells using microcarrier beads in a stirred bioreactor

Bone marrow mesenchymal stem cells (bmMSCs) have recently gained attention as a useful resource in the fields of regenerative medicine and tissue engineering. However, the number of bmMSCs obtained from available donors is very low. Here we developed a culture strategy for in vitro expansion of bmMSCs in a 1.5 L stirred bioreactor with microcarrier beads. First, the microcarriers (Cytodex 3) were equilibrated in culture medium containing 3% fetal bovine serum (FBS) for at least 30 min prior to cell addition. After inoculation, the FBS concentration of the medium was maintained at 3% (v/v) in the first 24 h and thereafter maintained at 1% (v/v) and a developed feeding regimen was applied over 5 days. The maximum cell density of 2.6 × 10⁶ cells/mL was achieved at day 5, corresponding to a 10.4 ± 0.8 fold increases in total cell number. Among the harvested cells, 98.95% expressed CD29 and 84.48% expressed CD90, suggesting that the majority of expanded bmMSCs still retained their differentiation potential. Therefore, the developed microcarrier-based stirred bioreactor culture system is an effective method to generate significant numbers of bmMSCs for potential applications and research studies.     

Optimization of monoclonal antibody production: combined effects of potassium acetate and perfusion in a stirred tank bioreactor

To increase the yield of monoclonal antibody in a hybridoma culture, it is important to optimize the combination of several factors including cell density, antibody productivity per cell, and the duration of the culture. Potassium acetate enhances the production of antibodies by cells but sometimes depresses cell density. The production of anti-(human B-type red blood cell surface antigen) antibody by Cp9B hybridoma was studied. In batch cultures, potassium acetate inhibited Cp9B cells growth and decreased the maximal cell density but the productivity of antibody per cell was increased. The balance of the two effects resulted in a slight decline of antibody production. In a stirred tank bioreactor, the inhibitory effect of potassium acetate on cell density was overcome by applying the perfusion technique with the attachment of a cell-recycling apparatus to the bioreactor. In such a reactor, potassium acetate at 1 g l^-1 did not cause a decrease in the cell density, and the antibody concentration in the culture supernatant was increased from 28 μg ml^-1 to 38 μg ml^-1. Potassium acetate also suppressed the consumption of glucose and the accumulation of lactate in batch cultures, but the glucose and lactate levels were kept stable by applying the perfusion technique in the stirred tank bioreactor. This revised version was published online in July 2006 with corrections to the Cover Date.     

Expansion of human mesenchymal stem cells on microcarriers

The effects on human mesenchymal stem cell growth of choosing either of two spinner flask impeller geometries, two microcarrier concentrations and two cell concentrations (seeding densities) were investigated. Cytodex 3 microcarriers were not damaged when held at the minimum speed, N_JS, for their suspension, using either impeller, nor was there any observable damage to the cells. The maximum cell density was achieved after 8–10 days of culture with up to a 20-fold expansion in terms of cells per microcarrier. An increase in microcarrier concentration or seeding density generally had a deleterious or neutral effect, as previously observed for human fibroblast cultures. The choice of impeller was significant, as was incorporation of a 1 day delay before agitation to allow initial attachment of cells. The best conditions for cell expansion on the microcarriers in the flasks were 3,000 microcarriers ml⁻¹ (ca. 1 g dry weight l⁻¹), a seeding density of 5 cells per microcarrier with a 1 day delay before agitation began at N_JS (30 rpm), using a horizontally suspended flea impeller with an added vertical paddle. These findings were interpreted using Kolmogorov’s theory of isotropic turbulence.     

Experiences with a new type of microcarrier

Summary Two new microcarriers were tested and showed good properties in cell attachment, cell growth and production of Human--Interferon. Cell densities up to 5·10⁶ cells/ml on microcarriers were reached in 1 l bioreactors.     

Transferrin recycling perfusion culture of hybridoma cells

A perfusion culture of hybridoma cells in serum-free medium recycling transferrin was carried out, which greatly reduced the level of transferrin that was needed. The culture was maintained even without supplying transferrin for nine days. IgG concentration reached 1.1 mg ml⁻¹ in a month of recycling and its ratio to the total protein was 45.8%. The affinity of the antibody did not decrease and no degradation was observed after long recycling period. The cell density under recycling condition was 2≈3 times higher than that without recycling. It was indicated that there was autocrine growth promoting activity in the culture supernatant.