Kinetics of producing pro-urokinase in perfusion cultivations

Summary Better production of pro-urokinase from human cell line was observed with 5% serum containing medium than 10% or serum free medium on Cytodex II under perfusion chemostat operations, showing 0.8×10^–5 (IU/daycell) of maximum productivity at 0.020 (l/h) of dilution rate in 5% serum medium, which corresponds to 800 IU/mL at this dilution rate. Conversion of pro-urokinase was reduced in the serum-containing media.     

Enhancement of the attachment on microcarriers and tPA production by fibroblast cells in a serum-free medium by the addition of the extracts ofCentella asiatica

The addition of ethanol extracts ofCentella asiatica showed a remarkable enhancement of fibroblast cells attachment to Cytodex beads in serum-free (SF) medium. It also improves tPA production in both batch and perfusion cultivations. The optimal concentration for SF medium was determined as 2 ppm of the extracts when using Cytodex III. In batch cultivation a high specific tPA production rate was obtained, compared to that from 5% FBS containing medium. However, a fast specific growth rate was observed in 5% FBS medium. In perfusion cultivation a reasonably good cell density and tPA production was achieved at a perfusion rate of 2.4×10⁶ (viable cell/ml) and 0.65 (g/ml), respectively at 22 ml/min.     

The economic production of anti-microbial factor from human promyelocytes in low serum containing medium under chemostat cultivation

It proves that a purifed Anti-Microbial Factor (AMF) from human promyelocytes has strong activity on Gram(–) and Gram(+) bacteria, showing 0.5 (g/ml) of Minimal Bacterical Concentration (MBC) on bothE. coli andS. aureus. For mass production of AMF, chemostat cultivation is recommended to accumulate cells out of the reactor since it is an intracellular protein and its system requires only 1% serum in the medium. Its production process proves to be closely growth-related. 1.7×10^–8 (g/viable cell/day) of maximum specific AMF production rate is estimated at 0.026 h^–1 of dilution rate, maintaining 6×10⁶ (viable cell/ml). Ca. 300 (mg/ml) of crude AMF can be obtained for 50 days of continuous cultivation under optimal conditions. The cell growth reaches relatively fast steady state.     

Feasibility study on the use of hyperosmolar medium for improved antibody production of hybridoma cells in a long-term,repeated-fed batch culture

To test the feasibility of using hyperosmolar medium for improved antibody production in a long-term, repeated fed-batch culture, the influence of various culture conditions (serum concentration and cultivation method) on the hybridoma cells' response to hyperosmotic stress resulting from sodium chloride addition was first investigated in a batch culture. The degree of cell growth depression resulting from hyperosmotic stress was dependent on serum concentrations and cultivation methods (static and agitated cultures). Depression of cell growth was most significant in agitated cultures with low serum concentration. However, regardless of serum concentrations and cultivation methods used, the hyperosmotic stress significantly increased specific antibody productivity (q _MAb). Increasing osmolality from 284 to 396 mOsm kg^–1 enhanced the q_MAb in agitated cultures with 1% serum by approximately 124% while the similar osmotic stress enhanced the q _MAb in static cultures with 10% serum by approximately 153%. Next, to determine whether this enhanced q_MAb resulting from hyperosmotic stress can be maintained after adaptation, long-term, repeated-fed batch cultures with hyperosmolar media were carried out. The cells appeared to adapt to hyperosmotic stress. When a hyperosmolar medium (10% serum, 403 mOsmkg^–1) was used, the specific growth rate improved gradually for the first four batches and thereafter, remained constant at 0.040±0.003 (average ± standard deviation) hr^–1 which is close to the value obtained from a standard medium (10% serum, 284 mOsmkg^–1) in the batch culture. While the cells were adpating to hyperosmotic stress, the q_MAb was gradually decreased from 0.388×10^–6 to 0.265×10^–6 g cell hr^–1 and thereafter, remained almost constant at 0.272±0.014× 10^–6 g cell^–1 hr^–1. However, this reduced q _MAb after adaptation is still approximately 98% higher than the q_MAb obtained from a standard medium in the batch culture.The authors would like to thank Dr.M. Kaminski for providing the hybridoma cell line used in this study. This work was supported by the Korea Science and Engineering Foundation.     

Long term and large-scale cultivation of human hepatoma Hep G2 cells in hollow fiber bioreactor

Long-term and large scale cultivation of an anchorage-dependent cell line using an industrial scale hollow fiber perfusion bioreactor is described. Hep G2 cells (a human hepatoma cell line) were cultivated in an Acysyst-P^® (Endotronic) with a total fiber surface area of 7.2 m² (6×1.2 m²) to produce Hep G2 crude conditioned medium (CCM). Pretreatment of the cellulose acetate hollow fibers with collagen enhances the attachment of the anchorage-dependent cells. We have succeeded in growing the Hep G2 cells in an antibiotics-and serum-free IMDM medium, supplemented with 50g/ml of Hep G2 CCM protein at inoculation. The Hep G2 cells replicate and secrete CCM protein in quantities comparable to those produced in DMEM containing 10% fetal calf serum (FCS). The highest CCM protein productivity during the 80-day cultivation was 1.1 g/day with a total of 30 g of protein accumulated. Hep G2 CCM (20–40 g protein/ml) was comparable to or even better than 10% FCS in supporting the growth of Molt-4 (a human T leukemia cell line) and FO (a mouse myeloma cell line) cells in vitro. The availability of this large amount of Hep G2 CCM will aid the further purification and characterization of growth factor(s) which could be used as serum substituents.     

Liposome mediated delivery of retinoids and aromatic polyamidines: Effects on growth of tumor cell lines

Ceramic pieces composed of 99.5% Al₂O₃, 3 to 6 mm long, were found to be a good matrix for growth of the human embryonic lung diploid fibroblast, IMR-90 cells. The tissue plasminogen activator (t-PA) was secreted in DME medium containing proteose peptone as a t-PA inducer. In addition, production of t-PA was enhanced by increasing extracellular CaCl₂, from 3.6 to 5.4 mM. In order to eliminate negative feed-back control caused by t-PA produced and thus raise productivity, perfusion cultivation was performed using a ceramic-packed bed column, with a recirculating vessel. The recirculating vessel was used to mix fresh medium with spent medium, and to control dissolved oxygen concentrations in the extracellular environment by stirring. In continuous production using the packed bed column with 2 kg of ceramics (Ø=H=150 mm), increasing dilution rate to 0.5 day^-1 could reduce product inhibition at 3–4×10⁵cells/ml. Cellular productivity of 560 IU/10⁶cells/day was obtained over 40 days and corresponded to the volumetric productivity of 183 IU/ml/day.Abbreviations CBR Ceramic Bed Reactor - Lv Linear Velocity     

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.     

Peptone,a low-cost growth-promoting nutrient for intensive animal cell culture

The effect of addition of peptone to serum-free and serum supplemented media for the growth of hybridoma cells in various systems was studied. Supplementation of defined medium with either proteose peptone or meat peptone resulted in significant increases in cell number and specific monoclonal antibody production in batch culture system. Other peptones were either inactive or less effective. In continuous culture, using medium supplemented with new born calf serum, the addition of peptone resulted in 125% and 150% increases in cell and antibody concentrations respectively. Similar increase in cell number (128%) was also obtained in spin-filter perfusion culture when medium was supplemented with peptone. By comparison, the substitution of a defined 1xMEM amino acids mixture resulted in only a 50% increase. At higher perfusion rates the cell number maintained in steady state using peptone supplement could be increased to 1.3×10⁷ cells ml^–1 while the serum concentration was reduced from 5% to 1% at a perfusion rate of 2.5 volumes per day.     

Evaluation of the new serum-free medium (MDSS2) for the production of different biologicals: Use of various cell lines

The presence of serum in cell culture raises safety problems for the production of biologicals, thus a new serum-free medium (MDSS2) was developed. The evaluation of this medium for the growth of different cell lines (BHK-21 C13, BSR and Vero) has shown that cells grew in this medium similarly to standard serum-containing medium, independently of the culture system used: in static (as monolayer) as well as in agitated systems (in suspension in spinner and perfusion reactors). BHK-21 and BSR cells grew as aggregate cultures and could proliferate in both static and agitated culture systems. Vero cells stayed attached to a substrate and proliferated equally in static and in agitated microcarrier-culture systems. The cell densities obtained with BHK-21 cells depended only on the culture system used. They ranged from 2–3×10⁶ to 6–12×10⁶ cells per ml for static batch and perfusion reactor cultures respectively. The cell concentration was 3 to 6 times higher than in classical cultures performed in serum-containing medium. The cell densities obtained with Vero cells were indistinguishable from those obtained in serum-containing medium, whatever the cell culture system used. These cell lines have been used for the production of rabies virus. With respect to BHK-21 and BSR, similar production rates of rabies glycoprotein have been found as in the standard roller bottle process. The production of rabies virus and of viral glycoprotein by Vero cells cultivated in serum-free medium was augmented 1.5-fold and 2.5-fold, respectively, when compared to serum-containing medium.A recombinant BHK-21 cell line, producing human IL-2, can also proliferate in MDSS2, after addition of insulin. The specific IL-2 production rate was augmented 3–4 fold in comparison to serum-containing medium.For the cells tested, the MDSS2 serum-free medium is a good growth and production medium. Its use for cultivating other cell lines and/or for the production of other biologicals is discussed.     

Plant regeneration from stem cortex protoplasts of Brassica napus

Cell layer strips composed of the epidermis and 7–9 layers of subepidermal cells were isolated from the 3–4 terminal internodes of Brassica napus cv Westar plants at the early flowering stage. The strips were precultured for one day in modified liquid MS [11] medium and subsequently incubated for 17–18 h in a 0.4 M mannitol solution containing 1% Macerozyme and 1% Cellulase Onozuka R-10. Protoplast yield was 2–2.8×10⁶ per 1.0g of tissue. Protoplasts were cultured at 1×10⁵/ml in three different media: S₁ [13], B [12] and L[8]. The first cell divisions occurred after 2–8 days of culture at frequencies of 20–54%. The highest growth rate of colonies was obtained in L medium containing 0.4 M sucrose and 2% Ficoll. After 4 weeks, green calli, 1–2 mm in diameter were transferred onto B₅ [2] medium with 3 mgl^-1 zeatin, 1% sucrose, 0.1 M mannitol and 0.5% agarose for shoot regeneration. Up to 20% of the calli regenerated shoots which subsequently were rooted and established in soil in the greenhouse.     

Effect of β-alanyl-L-histidinato zinc on differentiation of osteoblastic MC3T3-El cells: Increases in alkaline phosphatase activity and protein concentration

The effect of -alany-L-histidinato zinc (AHZ) on bone cell function was investigated in osteoblastic MC3T3-E1 cells. Cells were cultured for 3 days at 37°C in a CO₂ incubator in plastic dishes containing -modified minimum essential medium supplemented with 10% fetal bovine serum. After the cultures, the medium was exchanged for that containing 0.1% bovine serum albumin plus AHZ (10^–7–10^–5 M) or other reagents, and the cells were cultured further for appropriate periods of time. The presence of AHZ (10^–7–10^–5 M) produced a remarkable increase of alkaline phosphatase activity and protein concentration in osteoblastic cells. Thus increases were seen with the prolonged cultivation (12–21 days). With the culture of 1, 3 and 12 days, the effect of AHZ (10^–6 M) to increase alkaline phosphatase activity and protein concentration was more intensive than the effect of zinc sulfate, (10^–6 M). The AHZ effects were completely abolished by the presence of cycloheximide (10^–6 M), indicating that AHZ stimulates protein synthesis in the cells. The present study suggests that AHZ has a stimulatory effect on cell differentiation, and that this effect is partly involved on protein synthesis in osteoblastic cells.     

In vitro propagation of the bamboo (Bambusa tulda Roxb.) through shoot proliferation

An efficient protocol has been developed for the in vitro propagation of Bambusa tulda through shoot proliferation. Shoots from 3-week-old aseptically grown seedlings were used to initiate cultures. Multiple shoots were obtained on liquid Murashige and Skoog (MS) medium supplemented with 6-benzylaminopurine (8×10^–6M) and kinetin (4×10^–6M). Continuous shoot proliferation at a rate of 4–5 fold every three weeks was achieved through forced axillary branching. More than 90% of the shoots could be rooted on a modified MS medium containing indoleacetic acid (1×10^–5M) and coumarin (6.8×10^–5M). Following simple hardening procedures, the in vitro raised plants were transferred to the soil with more than 80% success.Abbreviations BAP 6-benzylaminopurine - 2-ip 6-,-dimethylallylaminopurine - Kn kinetin - IAA 3-indoleacetic acid - IBA 3-indolebutyric acid - NAA 1-naphthaleneacetic acid     

An ultramicro bioluminescence assay of enolase: Application to human cerebrospinal fluid

A highly sensitive method based on bioluminescence is described for the assay of enolase which can measure as little as 0.4×10^–6IU of activity. This corresponds to an amount of enzyme present in 1–2 l of normal human cerebrospinal fluid and is therefore easily applicable to clinical samples of CSF which can only be obtained in very small amounts. The reproducibility of the method is very high within a broad range of enzyme concentrations and the assay is linear from 0.4×10^–6 IU up to at least 50×10^–6IU of enzyme. This would permit application of the method to biological samples containing low as well as high enolase activities and especially for monitoring changes in enolase concentrations in the CSF and in the serum, as a function of pathological lesions in the central nervous system and other tissues.Part of this work was presented at the 2nd International Symposium on monoclonal antibodies and inborn errors of metabolism, Brugge, Belgium, October 1983.     

Isolation,culture and plantlet regeneration from cotyledon and mesophyll protoplasts of two pickling cucumber (Cucumis sativus L.) genotypes

Optimal protoplast yields from cotyledons (2.0×10⁶ protoplasts/ 0.5 g tissue) and from true leaves (5.0×10⁶ protoplasts/g tissue) of two Cucumis sativus genotypes were obtained following a 16 h digestion with, respectively, 1.25% pectinase+0.5% Cellulysin and 0.5 % pectinase+ 1.0% Cellulysin. Enzyme solutions were prepared in modified MS medium containing half-strength major salts, full complement of minor salts and vitamins, 2% sucrose and 0.25 M mannitol. A plating density of 3.5–4.0× 10⁴ protoplasts/ml or higher was required for sustained division, with first division occurring in 6–7 days, second-third division in 8–9 days, and minicalli formation by day 13. Embedding in 0.4% agarose provided the highest plating efficiency (proportion that formed minicalli) of mesophyll protoplasts, which was 28.3% for genotype 3672 and 15% for genotype 3676. By comparison, liquid culture and droplet culture gave lower plating efficiencies (10–19%). Cotyledon and mesophyll protoplasts of one genotype formed minicalli on MS medium containing 2,4-D/BA at 1.0/2.5 M and 5.0/5.0 M, respectively, within 21 days, while mesophyll protoplasts of the second genotype formed minicalli on MS medium containing NAA/BA at 5.0/5.0 M within 12 days. Shoot buds or somatic embryos were obtained upon subculture of calli to MS medium containing lower concentrations (0.05–0.01 M) of 2,4-D/BA or NAA/BA and a few plantlets, ca.18, were recovered on hormone-free medium.Abbreviations BA benzyladenine - 2,4-D 2,4-dichlorophenoxyacetic acid - MS Murashige and Skoog medium - NAA naphthaleneacetic acid     

Improved methods for investigating the external redox potential in hybridoma cell culture

Because of the interest in understanding and optimizing secretion of proteins from mammalian cells, reliable and more reproducible methods are needed to monitor the external redox potential of animal cells in suspension culture. An improved off-line method was established that greatly reduces the typically long response time of redox electrodes in cell culture media and improves the standardization of redox probes. In addition, the dependence of medium redox potential on dissolved oxygen concentrations and pH was investigated using cell-free medium. Off-line as well as on-line redox potential measurements were then applied to spinner or bioreactor cultures of murine hybridoma cells. Serum containing or protein-free medium were used. The time dependence of the experimentally determined external redox potential was found to be affected not only by oxygen, pH, and medium composition. but to a significant extent by the rate of generation of reductants by hybridoma cells. The observed specific rate of medium reduction by generation of reductants (mV h^–1 viable cell^–1) decreased during exponential growth while cell number increased from 2×10⁵ viable cells ml^–1 to 3.5×10⁶ viable cells ml^–1. This rate, however, was essentially constant at –7.3 mV h^–1±3.7 mV h^–1 per 10¹⁰ viable cells during growth under conditions of constant dissolved oxygen tension and constant pH. Using these observations, the quantity of reductants synthesized and secreted into the medium by viable hybridoma cells was estimated to be approximately 1.3 mole h^–1 per 10¹⁰ viable hybridoma cells. The time course of specific monoclonal antibody secretion rate did not correlate with changes in the external oxidation/reduction potential in either serum containing or protein-free medium.     

A photochemical fuel cell system using Anabaena N-7363

Summary A blue-green algae, Anabaena N-7363, was immobilized in 2% agar gel. The hydrogen productivity of the immobilized algae was three times higher than that of free algae. The maximum hydrogen production rate by the immobilized blue-green algae was 0.52 moles h^–1 g^–1 (of wet gel) in the medium without nitrogen sources under illumination (10,000 lux). The oxygen evolved was then removed by a reactor containing aerobic bacteria. A photo-current of 15–20 mA was continuously produced for 7 days by the photochemical fuel cell system consisting of the immobilized Anabaena reactor, the oxygen-removing reactor and the hydrogen-oxygen fuel cell. The conversion ratio of hydrogen to current was from 80% to 100%.     

Enhanced antibody production associated with altered amino acid metabolism in a hybridoma high-density perfusion culture established by gravity separation

A high density hybridoma perfusion culture was established by separating and recycling cells from the product stream to the reactor using a simple external sedimentation-based separator — an inclined modified Erlenmeyer flask. After 3 weeks, when the optimal perfusion rate of 1.0 day^–1 had been reached, viable cell density stabilized at around 10×10⁶ cells ml^–1, a level five times that obtained by simple batch culture. The efficiency of the separator was enhanced by cell flocculation. Specific antibody productivity, which was initially 0.4 g 1×10⁶ cells^–1 h^–1, decreased to half that value while cell density was increasing, but recovered to the initial level when the culture finally stabilized at a high cell density. During the final phase, when viable cell density and specific antibody production were high, there was a marked shift in metabolism. Consumption of the two most important substrates for energy generation, glucose and glutamine, caused their broth concentrations to decrease to 1.5 mM and 1 mM, respectively, from input medium concentrations of 25 mM and 10 mM, respectively. At the same time there was an increase in the specific production of glycine and aspartate, their broth concentrations reaching 1.5 mM and 0.02 mM, respectively. We suggest that this shift in metabolism results in enhanced production of ATP from glutamine. The specific glucose consumption and lactate production also indicate that there is a shift to more energy efficient metabolism. The mechanism whereby this leads to enhanced specific antibody production remains to be elucidated. Nevertheless, the combination of high cell density and enhanced productivity obtained with the present perfusion culture resulted in a high monoclonal antibody production –100 mg l^–1 d^–1.     

Growth characterizations of a human monocytic leukemia cell line in a serum-free medium

A clone, AH-01S, derived from a human monocytic leukemia cell line, THP-1, grew rapidly in a serum-free medium containing insulin, transferrin, ethanolamine, and sodium selenite. In batch culture using the serum-free medium, the AH-01S cells proliferated at a specific growth rate (μ) of 0.30 to 0.50 (1/day) from a cell concentration of 1 × 10⁴ cells/ml to 1.6 × 10⁶ cells/ml, an increase of 160 times. A higher cell concentration of 0.45 × 10⁷ cells/ml (cell volume ratio was 0.5%) was obtained in spinner flask culture using the serum-free medium. A mean specific growth rate 0.50 (1/day) was also observed in a culture in a fully instrumented cell culture fermentor. However, μ decreased drastically after the cell concentration reached 1.5 × 10⁶ cells/ml. Analyses of medium composition during cultivation revealed that under lower cell concentration, l-glutamine was the main carbon source while glucose was converted to lactate almost stoichiometrically, and that the production of lactate from glucose decreased at higher cell concentrations. To obtain cultures of 1 × 10⁹ cells, 1,200 to 1,300 mg of a carbon source (glucose) and 400 to 500 of amino acids were consumed during high cell concentration cultivation of the AH-01S cells in the serum-free medium.     

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