High-density culture of recombinant Chinese hamster ovary cells producing prothrombin in protein-free medium

A recombinant CHO cell line, CHO2DS, was immobilized on porous microcarrier Cytopore 1 and cultivated in 1 l modified Super-spinner and 2 l stirred tank bioreactor with the perfusion of a low-cost chemically defined protein-free medium DF6S. CHO2DS cells could enter into the inner space and grew both in the inner space and on the surface of Cytopore 1 in DF6S and produced prothrombin at 22 mg l^–1 after 10 days. From a seeding density of 5.7 × 10⁵ cells ml^–1, the highest viable cell density of CHO2DS was 1.12 × 10⁷ cells ml^–1.     

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     

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.     

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     

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     

用改装的Ｓuper—Spinner搅拌瓶连续灌流培养产凝血酶原ＣＨＯ工程细胞

在动物细胞培养过程中对培养体系实施培基连续灌流能及时地补充细胞生长所需的营养物质、控制细胞代谢产物对细胞的影响 ,实现细胞的高密度长期培养 ,提高目的产品的生产效率[1,2 ] 。细胞连续灌流培养的前提是在实施培基连续灌流的同时培养体系能有效地截留细胞[3] 。这一前提增加了细胞培养装置的复杂程度 ,使之特化为价格昂贵的生物反应器 ,限制了细胞连续灌流培养的应用。如能通过对普通的细胞搅拌培养瓶进行改进 ,使之能用于细胞的连续灌流培养 ,则有利于细胞连续灌流培养的推广应用。1　材料和方法1 1　细胞产人重组凝血酶原ＣＨＯ工…     

Establishment of callus and cell suspension cultures from Gypsophila paniculata leaf segments and study of the attachment of host cells by Erwinia herbicola pv. gypsophilae

Callus and cell suspension cultures were initiated from leaf segments of G. paniculata. Fresh and dry weights measurements of callus showed that callus growth was optimal on MS medium supplemented with 1.0 mg l^–1 2,4-dichlorophenoxyacetic acid (2,4-D) and 0.2 mg l^–1 benzyladenin (BA). Calli cultured on this medium, showed a two-fold increase in fresh weight by the fourth week of incubation. The initiated hard green callus was repeatedly subcultured on MS medium containing increasing concentrations of 2,4-D in order to increase its friability. The friable callus was then used for establishment of a cell suspension culture. Maximum growth of the suspension culture was on medium supplemented with 1.0 mg l^–1 2,4-D and 0.2 mg l^–1 BA.The suspension culture was used for studying plant host attachment in both electron and light microscopy. Upon infection with E. herbicola, plant cells showed aggregate formation within 24 h of infection. In the presence of the pathogenic Ehg,the number of aggregates formed was 342 aggregates ml^–1, in the presence of the non-pathogenic Ehg154 aggregates ml^–1 and in the control 115 aggregates ml^–1. These results show that the pathogenic strain causes formation of cell aggregates 5.8 times greater than the non-pathogenic one. Based on these results, it can be hypothesized that bacterial cells of the pathogenic strains bind to the plant cells and may form a bridge for attachment of plant cells to one another. Observations by electron microscope show that bacterial cells do attach to plant cells and that this attachment might be via formation of a bridge between the bacteria and the plant cell.     

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.     

Improved yields of the extracellular domain of the epidermal growth factor receptor produced using the baculovirus expression system by medium replacement following infection

The extracellular domain of the epidermal growth factor receptor (EGFR) was expressed using the baculovirus expression vector system. The maximum level of the EGFR extracellular domain secreted into the medium in Sf-9 (Spodoptera frugiperda or fall armyworm) cell batch culture was approximately 2.5 g ml^–1. In order to increase this yield, a process was developed that included the following sequence of steps: batch growth to maximum cell density, infection of the cells with recombinant virus, and replacement of spent medium. By using this process, the specific yield of recombinant protein, which in batch culture drops when infection is carried out at densities greater than 3 × 10⁶ cells ml^–1, can be maintained at a maximum in cultures infected at densities of 10⁷ cells ml^–1 or greater. The process, when applied to 3-1 and 11-1 bioreactor cultures, allowed a maximum volumetric yield of triple the maximum value attainable in batch culture. Spent-medium analysis indicates that medium replacement provides certain nutrients that could otherwise be limiting for recombinant protein production.     

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.     

Callus and suspension cultures for biomass production ofCynara cardunculus (Compositae)

Summary Friable calli, obtained from hypocotyl and leaf segments ofCynara cardunculus, were used for the production of cell suspension cultures in liquid Gamborg B₅ medium supplemented as for callus obtention. The low inoculum cell suspension cultures (6.9×10⁴ cells.ml^–1) presented a td=136.8 hours while those obtained with a high inoculum (15.6×10⁴ cells.ml^–1) reached a td=33.6 hours.     

Interleukin-6 is antiproliferative to a mouse hybridoma cell line and promotive for its antibody productivity

Monoclonal antibody production by hybridoma cells at moderately slowed growth states would be favorable for commercial scale production since cells can devote their resources to performing the differentiated function, immunoglobulin production. We found that a purified recombinant human interleukin-6, which had been reported to support or stimulate proliferation of B cell hybridoma/plasmacytoma cells, suppressed growth of a hybridoma cell line in serum-free medium. In the presence of the interleukin, the growth-suppressed cells were viable for remarkably long periods in batch culture, and after removal of the interleukin from the culture medium, they started to proliferate at their normal growth rate. As the concentration of the interleukin increased in the culture, the growth rate decreased and the specific antibody productivity (antibody production rate per cell) increased to 5-fold of control at 10 U ml^–1 (2 ng ml^–1) of the interleukin.Abbreviations IL-1,2, and 6 interleukin-1, 2 and 6 - rhIL-6 recombinant human interleukin-6 - MCAb monoclonal antibody - TNP trinitrophenyl - unit (U) of interleukin-6 A unit (U) is equivalent to the amounts of IL-6 which gives one-half maximal IgM secretion by SKW6-CL4 cells (1U ml^–1=200 pg ml^–1)     

Propagation ofSpodoptera frugiperda cells (Sf9) and production of recombinant proteins with the baculovirus expression system using improved spinner flasks with membrane aeration

Summary It has been shown that the growth of Spodoptera frugiperda cells is significantly reduced or ceased under oxygen limiting culture conditions. This paper describes the use of a new membrane-aerated spinner flask which was compared to conventional surface-aerated spinner flasks with regard to growth of the insect cell line Sf9 and recombinant protein production after infection with baculovirus. Using a commercially available serum-free culture medium Sf9 cells reached highest cell densities (3×10⁶ ml^–1) in the membrane-aerated spinner flask. Production of recombinant protein was also influenced by the oxygen supply. In the membrane-aerated spinner flask and in a surface-aerated spinner flask with reduced filling volume more than 20000 U ml^–1 of a recombinant interleukin-2 variant were accumulated whereas only 100 U ml^–1 were produced in a surface-aerated spinner flask with insufficient oxygen supply. Sufficient oxygenation appears to be essential for proliferation of Sf9 cells as well as recombinant protein production after infection with baculovirus. Membrane oxygenation allows sufficient oxygen supply at high cell density and an at least 2.5 fold higher filling volume per spinner unit.     

Plant regeneration through direct somatic embryogenesis from protoplasts of banana (Musa spp.)

Summary We report the isolation and regeneration of protoplasts from an embryogenic banana (Musa spp.) cell suspension culture initiated from in vitro proliferating meristems. A high yielding isolation method (up to 6×10⁷ protoplasts.ml^–1 packed cells) is discussed. Optimal regeneration, with more than 50% of the protoplasts showing initial cell division, occurred when high inoculation densities (10⁶ protoplasts.ml^–1) or nurse cultures were applied. Under these conditions, the frequency of microcolony formation was 20–40%. These microcolonies developed directly, without an intervening callus phase, into somatic embryos which later germinated and formed plantlets.     

The maintenance ofBdellovibrio at low prey density

A mathematical model for the interaction ofBdellovibrio and its prey predicted that a relatively high prey density (7×10⁵ cells ml^–1) would be required for the establishment of an equilibrium in a mixed population [8]. The present report shows thatBdellovibrio can be maintained in a continuous culture when the prey cell density is much lower (2–5×10⁴ cells ml^–1), and closer to that of naturally occurring bacterial populations in sea waters.     

Lifetable demography of four cladoceran species in relation to algal food (Chlorella vulgaris) density

Algal food density is known to influence life history variables of cladoceran species. It is not, however, well established whether both littoral and planktonic cladocerans show similar trends when exposed to increasing food concentrations. In the present work, we studied the life table demography of four cladoceran species (Ceriodaphnia cornuta, Moina macrocopa, Pleuroxus aduncus and Simocephalus vetulus) in relation to three algal food concentrations (low: 0.5 × 10⁶, medium: 1.5 × 10⁶ and high: 4.5 × 10⁶ cells ml^–1 of Chlorella vulgaris) (in terms of carbon content, these were equivalent to 0.15, 0.45 and 1.35 g ml^–1, respectively) at 25 °C. In general, for all the tested cladoceran species, values of average lifespan, gross reproductive rate, net reproductive rate, generation time and the rate of population growth were higher at lower food concentrations. Furthermore, high food concentration resulted in a negative population growth rate (mean ± standard error: –0.091 ± 0.026) for P. aduncus. The highest population growth rate (0.602 ± 0.014) was recorded for M. macrocopa at low food density. S. vetulus had the longest average lifespan (40 ± 1 d) while M. macrocopa had the lowest (5 ± 1 d). C. cornuta showed better performance at medium food concentration. We conclude that among the algal concentrations used here, 0.5 × 10⁶ – 1.5 × 10⁶ was beneficial not only to the planktonic species but also to the littoral P. aduncus and S. vetulus while 4.5 × 10⁶ cells ml^–1 was unsuitable for all the cladocerans tested.     

Large-scale perfusion culture process for suspended mammalian cells that uses a centrifuge with multiple settling zones

A high-cell-density perfusion culture process, using a novel centrifuge, was developed. The centrifuge has spiral multiple settling zones to separate cells from culture medium. Because of the multiple zones, the separation area can be efficiently increased without enlarging the diameter of the centrifuge. The centrifuge used in this study had a separation capacity of 2600 ml culture medium min^–1 at 100g of the centrifugal force. A new cell separation and withdrawal method was also developed. The cells separated in the centrifuge can be withdrawn easily from the centrifuge with no cell clogging by feeding a liquid carrier such as a perfluorocarbon into the centrifuge and pushing the cells out with the liquid carrier. By this culture process, monoclonal antibodies were produced with mouse-human hybridoma X87X at a cell density of about 8 × 10⁶ cells ml^–1 for 25 days. This centrifuge culture shows promise as a large-scale perfusion culture process.     

A study of the suspended algae in the River Derwent,Derbyshire, U.K.

Studies of the composition and abundance of algae suspended in the water of the River Derwent, Derbyshire, were made during 1983. Samples were collected at intervals of 2–3 weeks from 6 sites on the lower reaches of the river. Variations in both composition and abundance of suspended algae occurred with variations in flow. At the uppermost sites cell densities were generally low (<500 cells ml^–1) and the algae consisted mainly of dislodged benthic diatoms. The density in suspension of these algae of benthic origin increased with flow. At downstream sites a true potamoplankton developed; during the summer this consisted chiefly of centric diatoms with Chlorophyta and Cryptophyta. Even at the lowermost site, the maximum recorded density of cells (3 860 cells ml^–1) and cell load (30 × 10⁹ cells s^–1) were lower in the Derwent than in some other British rivers. However, the cell density could still represent a substantial part (up to 32%) of the total particle density in the river.     

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.     

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.