Continuous culture of CHO-K1 cells producing thrombomodulin and estimation of culture conditions

Recombinant Chinese hamster ovary (CHO-K1) cells expressing human soluble thrombomodulin (rsTM) were cultured in a continuous culture system with a fluidized-bed reactor. Cells were grown in a medium containing 1% serum for 10 d, and then cultured in a serum-free medium. The protein production rate increased remarkably in the serum-free culture, with a decrease in the lactate production rate. This suggests that CHO-K1 cells exhibit different physiological characteristics in response to serum removal from the medium, which resulted in a higher rsTM concentration (about 60 mg/l). A procedure for estimating protein productivity was developed using experimental glucose and lactate measurements. In this procedure, cell density was estimated from the glucose consumption rate, and the specific protein (rsTM) production rate was obtained from the ratio of lactate production/glucose consumption (ΔL/ΔG). Since the cell density and protein productivity in repeated batch culture were well estimated, the procedure was applied to continuous culture in a fluidized-bed bioreactor culture. The estimation procedure was also found to be effective in this continuous culture using the models derived from the repeated batch culture.     

Growth and differentiation of epidermal cells from the rainbow trout established as explants and maintained in various media

Growth and a number of differentiated characteristics of cultured epidermal cells from the rainbow trout Oncorhynchus mykiss were compared using two commercially available serum–free media, a dermal substrate/serum free kit and a serum–containing medium which had been previously optimized for epidermal cell culture. Each medium supported short term growth over 15 days. Only the medium supplied for dermal substrate culture supported longer growth periods. This medium was supplied for use with a collagen/stromal substrate but gave good cultures even without the substrate. Differentiation, measured by examining mucous cells, cytokeratins, epidermal growth factor receptor, gap junction status and ultrastructure showed that serum–free media gave quantitatively and qualitatively superior expression and short term retention of differentiation over serum–containing medium. Epithelial cell growth with expression of differentiated characteristics can be maintained in primary culture in serum–free medium for at least as long as in serum–containing medium. This provides a useful technique for use when serum presence in medium is undesirable or proves toxic to the specialized cell type under investigation.     

Evaluation of a simple protein free medium that supports high levels of monoclonal antibody production

A simple protein free medium was formulated and tested in suspension culture using three hybridoma cell lines. The medium, referred to as CDSS (Chemically Defined Serum Substitutes), consisted of the basal medium DMEM:Ham F12, 1:1, with HEPES (D12H), plus pluronic F68, trace elements, ferric citrate, ascorbic acid, and ethanolamine. No protein or lipid components were added. All three cell lines were weaned off serum using CDSS and a commercially available protein free medium PFHM-II. Data shown here indicated that normally cells took 1–7 weeks to wean off serum and an additional 2–7 weeks to adapt to suspension culture. After adaptation the cells were able to grow well in suspension culture using both protein free media and in the main performed better than serum containing controls. The stability of the three hybridoma cells for antibody production following freeze/thaw procedures and long term subculturing was also tested. All three lines were frozen using our protein free CDSS medium (containing 0.75% bovine serum albumin and 10% dimethyl sulfoxide) in liquid nitrogen for up to one year. Cells thawed from these stocks recovered well and were able to maintain good growth and antibody production characteristics. One line was shown to grow using our protein free CDSS medium in suspension culture for 12 weeks without loss of antibody productivity.     

Extension of Sp2/0 hybridoma cell viability through interleukin-6 supplementation

Sp2/0 hybridoma cells die principally by apoptosis in batch culture. We have found that cultures of the Sp2/0 hybridoma exhibit increased viability in response to interleukin 6 (IL-6) supplementation relative to control cultures during serum shiftdown experiments. When shifted from a medium containing 10% fetal bovine serum (FBS) to a medium with 1% FBS, IL-6 supplemented cultures displayed viabilities and viable cell densities similar to control cultures containing 10% FBS. The degree of the survival response induced varied in accordance with the severity of the shiftdown, as cells resuspended in a high serum medium showed little observable enhancement in viability. The extension in culture viability was not accompanied by an observable decrease in growth relative to control cultures, indicating that the effect was not a consequence of growth inhibition. These results suggest the existence of serum components with behavior functionally similar to IL-6, with respect to enhancing cell survival, and that under certain experimental conditions IL-6 serves as a survival factor. In contrast to the extended viability displayed by cultures supplemented with IL-6, Sp2/0 cultures transfected with IL-6 cDNA expression vectors displayed a growth inhibitory response relative to control cultures. This inhibitory response was characterized by an extended lag phase following inoculation, and a decrease in batch culture cell yield. The depression in cell yield varied with serum concentration, with the largest depression occurring at high serum concentrations. We conclude that interactions between components in serum, presumably growth factors, and cytokines play an important role in altering the behavior of industrially relevant cell lines in culture. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 439-446, 1997.     

Modeling and optimization of the baculovirus expression vector system in batch suspension culture

A mathematical model has been developed that predicts the cell population dynamics and production of recombinant protein and infective extracellular virus progeny by insect cells after infection with baculovirus in batch suspension culture. Infection in the model is based on the rate of virus attachment to suspended insect cells under culture conditions. The model links the events following infection with the sequence of gene expression in the baculovirus replicative cycle. Substrate depletion is used to account for the decrease in product yield observed when infecting at high cell densities. Model parameters were determined in shaker flasks for two media: serum-supplemented IPL-41 medium and serum free Sf900II medium. There was good agreement between model predictions and the results from an independent series of experiments performed to validate the mode. The model predicted: (1) the optimal time of infection at high multiplicity of infection: (2) the timing and magnitude of recombinant protein production in a 2-L bioreactor; and (3) the timing and magnitude of recombinant protein production at multiplicities of infection from 0.01 to 100 plaque-forming units per cell. Through its ability to predict optimal infection strategies in batch suspension culture, the model has use in the design and optimization of large-scale systems for the production of recombinant products using the baculovirus expression vector system. (c) 1994 John Wiley & Sons, Inc.     

Feasibility study on the use of calcium alginate-entrapped hybridoma cells for IgM production

In order to test the feasibility of using calcium alginate-entrapped hybridoma cells for IgM production, HO-22-1 hybridoma cells entrapped into calcium alginate beads with varying alginate concentrations were cultivated in spinner flasks. It was observed that the IgM produced by the entrapped cells could diffuse out of the calcium alginate beads regardless of alginate concentrations tested (0.8–2.5%). Since the increase in alginate concentrations showed an adverse effect on cell growth and maximum cell concentration, the use of lower alginate concentration was desirable for higher volumetric monoclonal antibody (MAb) productivity. When the entrapped cells in 0.8% alginate beads were cultivated in repeated-fed batch mode, the reduction of serum concentration in the medium from 10% to 1% did not decrease the volumetric IgM production. Taken together, the data obtained here showed the feasibility of using calcium alginate-entrapped hybridoma cells for IgM production.Alginate was generously provided by the Kelco company. This work was supported by the Ministry of Science and Technology, Korea.     

The growth factor inhibitor suramin reduces apoptosis and cell aggregation in protein-free CHO cell batch cultures

We have previously shown that Chinese hamster ovary (CHO) cells capable of growing in medium free of exogenous proteins die by apoptosis during all stages of a batch culture (Zanghi et al., 1999). On the basis of the hypothesis that extracellular death factors might be important in apoptosis under these conditions, we examined the effect of the growth factor inhibitor and antitumor agent suramin on CHO cell growth and apoptosis in serum-free culture. Suramin protected against apoptosis during exponential growth, as indicated by the absence of DNA laddering and an increase in cell viability from roughly 70% to above 95%. Suramin also effectively dispersed cell aggregates so that single-cell suspension culture was possible. However, suramin did not protect against apoptosis during the death phase, in contrast to serum, suggesting that antiapoptotic factors in the serum remain to be discovered. The increased viable cell yield following suramin supplementation resulted in a 40% increase in product yield, based on results with cells expressing recombinant secreted alkaline phosphatase. Polysulfated compounds dextran sulfate and polyvinyl sulfate worked nearly as well as suramin in dispersing cell clumps and increasing viable cell yield, which implies that suramin's high sulfate group density may be responsible for its effects in cell culture. In addition, suramin was beneficial for long-term adaptation of CHO cells to protein-free media suspension culture, and the compound was synergistic with insulin in accelerating this adaptation time.     

Functional differentiation and primary metabolism of mouse mammary epithelial cells in extended-batch and hollow-fiber culture

Growth, expression of functional differentiation (as characterized by synthesis and secretion of milk proteins), and primary metabolism were studied for a mouse mammary epithelial cell line, COMMA-1D, in extended-batch and hollow-fiber reactor cultures. Batch cultures were performed on Costar polycarbonate membrane inserts, allowing basal and apical exposure to medium. Protein production was induced in both batch and hollow-fiber cultures in hormonesupplemented medium. In batch cultures, high levels of protein production and secretion were maintained for 18 days. Once differentiation was induced, the rate of deinduction was low, even in medium containing epidermal growth factor (EGF) and serum; cells continued to express and secrete proteins for at least 12 days after prolactin and hydrocortisone were removed. Cells in both batch and hollow-fiber cultures were highly glycolytic and exhibited low rates of glutaminolysis. In batch culture on membrane inserts, cells showed polarized metabolism between the apical and basal side, maintaining significant gradients of glucose and lactate. Medium hormonal composition and subsequent differentiation affected both glucose uptake and lactate yield for COMMA-1D in batch culture. (c) 1992 John Wiley & Sons, Inc.     

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.     

Preparation of pure monoclonal antibody to interleukin-2 by cultivation of hybridoma cells entrapped in novel composite hydrogel beads

A simple and reliable technique was developed to prepare pure monoclonal antibody (MAb) to interleukin-2 using cells entrapped in novel composite poly(N-vinyl caprolactam)-calcium alginate beads. Flow cytometry was applied to study cell size and cell cytoplasm granularity distribution. Maximum MAb production by the gel-entrapped cells in serum free medium was 2-3-fold higher compared to free suspension culture in serum containing medium. The only contaminating protein in culture supernatant was transferrin at 5% w/v.     

Three-dimensional culture of human tumor cells under standardized medium conditions

The 3-dimensional culture of human tumor spheroids under standardized medium conditions may reveal information on specific biological parameters that could be masked in serum-supplemented media. Spheroids derived from human tumor cells are growth retarded in media free of serum. Ex-Cyte IV is a substance derived from human blood that can be used to improve growth in tissue culture. In this study the growth of spheroids from four different human tumor cell lines was studied when grown in medium free of serum, medium supplemented with varying concentrations Ex-Cyte IV, and medium supplemented with foetal calf serum (FCS). The parameters used for comparisons were growth rate, growth enhancement, clonogenicity and cell cycle distribution.The four cell lines showed different growth rates in serum-free medium, which were increased to different extents when Ex-Cyte IV or FCS were added. The growth enhancing effect induced by Ex-Cyte IV was differently concentration dependent for each cell line. The clonogenicity of cells grown as spheroids in serum-free medium was lower than in spheroids grown in supplemented media. There was no difference in clonogenicity between the differently supplemented media. All four cell lines responded to growth in serum-free medium with a drop in the S-phase and G2M phase.The present study provides a novel approach to the study of human tumor cells in 3-dimensional culture under defined conditions. The human serum derived substance Ex-Cyte IV may provide a method to obtain information on specific biological parameters that could be masked in serum-supplemented media.     

Development of Animal-free, Protein-Free and Chemically-Defined Media for NS0 Cell Culture

There has been a recent boom of monoclonal antibodies on the market, and a significant portion of them were produced by NS0 cell lines. As regulations become more stringent in ensuring production processes are free of potential contamination by adventitious agents, it is highly desirable to further develop serum-free media into ones that do not contain any components of animal origin, or ‘animal-free media’. Using a shake-flask batch culture system, recombinant proteins (human albumin and human insulin) and synthetic compounds (tropolone and ferric ammonium citrate) were identified to be capable of replacing the animal-sourced proteins commonly found in serum-free media for NS0 cell culture, namely bovine albumin, insulin and transferrin. The cholesterol requirement of NS0 cells was satisfied by the use of a commercially available non-proteinaceous, non-animal sourced cholesterol/fatty acid mix in place of bovine lipoproteins, which in effect also eliminated the need for recombinant albumin. In the animal-free medium thus formulated, NS0 cell lines, either the host or recombinant constructs, were all able to grow in batch culture to 1~ 3×10⁶ viable cells/ml for multiple passages, with no requirement for gradual adaptation even when seeded from 10% serum-containing cultures. It was surprising to observe that the recombinant insulin was essentially ineffective as sodium salt compared to its zinc salt. Studies showed that the zinc deficiency in the former resulted in a rapid decline of cell viabilities. Supplementation of zinc ions greatly improved growth, and even led to the total replacement of recombinant insulin and hence the formulation of a protein-free medium. When the cell lines were adapted to cholesterol-independent growth which eliminated the need for any lipid source, a completely chemically-defined animal-free medium was formulated. In all cases, antibody production by various GS-NS0 constructs in animal-free media was stable for multiple passages and at least similar to the original serum-free medium containing the animal-sourced proteins. The medium also served well for cryopreservation of NS0 cells in the absence of serum.     

Polyamine metabolism and gene regulation during the transition of autonomous sugar beet cells in suspension culture from quiescence to division

Sugar beet cells grown in batch suspension culture have been used to study the regulation of polyamine levels during the transition from a quiescent to a proliferating state. The quiescent state was achieved by maintenance of the phytohormone autonomous cells in the stationary phase of the batch culture cycle. After subculture into fresh medium there was an increase in DNA synthesis which was accompanied by a dramatic increase in cellular polyamine levels. The levels of both free and bound cellular putrescine and spermidine within the cells reached a peak before the onset of the first synchronous division. The levels of putrescine, spermidine and to some extent spermine in the culture medium also increased dramatically shortly after subculture. The increase in polyamines was preceded by a rapid but transient increase in omithine decarboxylase (EC 4.1.1.17) and S -adenosylmethionine decarboxylase (EC 4.1.1.50). Arginine decarboxylase (EC 4.1.1.19) and S -adenosylmethionine synthetase (EC 2.5.1.6) activity did not show the same pattern of cell division-related variation. Inhibition of S -adenosylmethionine biosynthesis with methylglyoxal bis-(guanylhydra-zone) (MGBG) reduced cell division in the suspension culture. Inhibitors of ornithine decarboxylase and arginine decarboxylase individually had little effect on cell division, but in combination led to a reduction in cell division. Addition of polyamines and their precursors to cells in the stationary phase of a batch culture cycle led to the induction of expression of a mitotic cyclin sequence ( BvcycII ).     

Polyamine metabolism and gene regulation during the transition of autonomous sugar beet cells in suspension culture from quiescence to division

Sugar beet cells grown in batch suspension culture have been used to study the regulation of polyamine levels during the transition from a quiescent to a proliferating state. The quiescent state was achieved by maintenance of the phytohormone autonomous cells in the stationary phase of the batch culture cycle. After subculture into fresh medium there was an increase in DNA synthesis which was accompanied by a dramatic increase in cellular polyamine levels. The levels of both free and bound cellular putrescine and spermidine within the cells reached a peak before the onset of the first synchronous division. The levels of putrescine, spermidine and to some extent spermine in the culture medium also increased dramatically shortly after subculture. The increase in polyamines was preceded by a rapid but transient increase in omithine decarboxylase (EC 4.1.1.17) and S -adenosylmethionine decarboxylase (EC 4.1.1.50). Arginine decarboxylase (EC 4.1.1.19) and S -adenosylmethionine synthetase (EC 2.5.1.6) activity did not show the same pattern of cell division-related variation. Inhibition of S -adenosylmethionine biosynthesis with methylglyoxal bis-(guanylhydra-zone) (MGBG) reduced cell division in the suspension culture. Inhibitors of ornithine decarboxylase and arginine decarboxylase individually had little effect on cell division, but in combination led to a reduction in cell division. Addition of polyamines and their precursors to cells in the stationary phase of a batch culture cycle led to the induction of expression of a mitotic cyclin sequence ( Bvcycll ).     

Media and environmental effects on phenolics production from tobacco cell cultures

The effects of various factors in culture medium on the phenolics production from cultured tobacco cells (free and immobilized) were studied. It was found that removing the growth hormone from the medium increased the productivities of phenolics for both free and immobilized cultures. Low initial sucrose concentration in the medium restricted growth and resulted in high cellular productivities of the phenolics for freely suspended cells, but not for the immobilized cells. Addition of 1.4% DMSO to standard culture medium greatly increased phenolics productivities without affecting cell viability in both free and immobilized cell cultures. Continuous operation of a packed-column reactor of the immobilized cells was achieved for 500 hours. Aeration was accomplished by diffusing pure oxygen through silicone tubing placed inside the reactor. It was found that prolonged cell viability was contingent upon initially operating the reactor with total recycle for several days, and then introducing fresh feed while maintaining a high recycle rate. Immobilized cells packed in a continuous column reactor achieved productivities more than twice that achieved in any batch run.     

Cell metabolism measurements in culture via microelectronic biosensors

Serum free fermentation procedures of cell cultures have got a wide application in production of biochemicals. But, cells cultured in serum free media in general are more sensitive to changes in culture condition, especially to nutrient limitation. There are no substances from serum which can support the cells when conditions are changing. In this study special attention is directed to amino acid utilization of mouse hybridoma in batch, chemostat and perfusion fermentations. Detailed data are presented which show the considerable difference of amino acid consumption rates in different fermentation modes. Already, in batch mode there are differences of the two investigated mouse hybridoma cell lines, although they are derived from the same myeloma line. In chemostat running at a dilution rate representing maximal growth rate most of the consumption rates are significant higher than in batch. On the other hand, in perfusion mode the rates are lower than in batch. This indicates clearly the different conditions of the fermentation modes. Therefore, it is necessary to develop serum free processes under the desired production conditions. An accurate analysis of the process is strongly recommended.     

Perfusion strategy for rosmarinic acid production by Anchusa officinalis

The production of an intracellular secondary metabolite rosmarinic acid (RA) by plant cell suspensions of Anchusa officinalis cultivated with intermittent medium exchange is investigated. Initially, a two-stage perfusion culture method was employed. After being cultured in the batch mode for ca. 6 days in B5 medium plus 3% sucrose, 1 mg/L 2,4-dichlorophenoxyacetic acid (2,4-D), and 0.1 mg/L kinetin (2,4-D B5 medium), Anchusa culture was cultivated to high cell density by perfusion during the growth stage using a hormone-free Gamborg B5 medium supplemented with 6% sucrose. This was followed by a production stage, in which a complete medium exchange into B5 medium plus 3% sucrose and 0.25 mg/L naphthleneacetic acid (NAA) was conducted. The two-stage perfusion culture had a higher maximum culture RA concentration but a lower RA content per cell than the batch stock culture maintained in the 2,4-D B5 medium. Higher culture RA concentration was due primarily to high cell density. The high packed cell volume, however, seemed to reduce the synergistic effect of NAA on RA synthesis. Subsequently, a single-stage perfusion culture method was investigated. The best result was obtained by growing the culture in the batch mode for ca. 10 days using B5 medium supplemented with 3% sucrose and 0.25 mg/L NAA, followed by perfusing the culture with B5 medium plus 6% sucrose and 0.25 mg/L NAA at a constant perfusion rate of 0.1/day. A maximum cell dry weight of 35 g/L and a RA concentration of almost 4 g/L were achieved. This is the highest RA concentration ever reported in the Anchusa culture. (c) 1993 John Wiley & Sons, Inc.     

Changes in monoclonal antibody productivity of recombinant BHK cells immobilized in collagen gel particles

Animal cell perfusion high density culture is often adopted for the production of biologicals in industry. In high density culture sometimes the productivity of biologicals has been found to be enhanced. Especially in immobilized animal cell culture, significant increase in the productivity has been reported. We have found that the specific monoclonal antibody (MAb) productivity of an immobilized hybridoma cell is enhanced more than double. Several examples of enhancing productivities have been also shown by collagen immobilized cells. Immobilized cells involve some different points from non-immobilized cells in high density culture: In immobilized culture, some cells are contacted together, resulting in locally much higher cell concentration more than 10⁸ cells/ml. Information originating from a cell can be easily transduced to the others in immobilized culture because the distance between cells is much nearer. Here we have performed collagen gel immobilized culture of recombinant BHK cells which produce a human IgG monoclonal antibody in a protein-free medium for more than three months. In this high density culture a stabilized monoclonal antibody production was found with around 8 times higher specific monoclonal antibody productivity compared with that in a batch serum containing culture. No higher MAb productivity was observed using a conditioned medium which was obtained from the high density culture, indicating that no components secreted from the immobilized cells work for enhancing monoclonal antibody production. The MAb productivity by the non-immobilized cells obtained by dissolving collagen using a collagenase gradually decreased and returned to the original level in the batch culture using a fresh medium. This suggests that the direct contact of the cells or a very close distance between the cells has something to do with the enhancement of the MAb productivity, and the higher productivity is kept for a while in each cell after they are drawn apart.     

A serum substitute for fed-batch culturing of hybridoma cells

We developed a substitute for serum to produce fed-batch cultures of hybridoma cells in serum-free medium and confirmed that the cells could be successfully cultivated this way. Our substitute consisted of 12 components. The specific production rates of lactate and ammonia, which are harmful byproducts from the cells, were significantly reduced compared with a conventional serum-containing batch culture. This reduction led to a higher cell concentration and a longer production lifetime. As a result, the final concentration of monoclonal antibody was 400 mg/L, or five times greater than that in the conventional serum-containing batch culture. The developed substitute is expected to enable fed-batch cultivation in a serum-free condition.     

Process development of human multipotent stromal cell microcarrier culture using an automated high‐throughput microbioreactor

Microbioreactors play a critical role in process development as they reduce reagent requirements and can facilitate high‐throughput screening of process parameters and culture conditions. Here, we have demonstrated and explained in detail, for the first time, the amenability of the automated ambr15 cell culture microbioreactor system for the development of scalable adherent human mesenchymal multipotent stromal/stem cell (hMSC) microcarrier culture processes. This was achieved by first improving suspension and mixing of the microcarriers and then improving cell attachment thereby reducing the initial growth lag phase. The latter was achieved by using only 50% of the final working volume of medium for the first 24 h and using an intermittent agitation strategy. These changes resulted in >150% increase in viable cell density after 24 h compared to the original process (no agitation for 24 h and 100% working volume). Using the same methodology as in the ambr15, similar improvements were obtained with larger scale spinner flask studies. Finally, this improved bioprocess methodology based on a serum‐based medium was applied to a serum‐free process in the ambr15, resulting in >250% increase in yield compared to the serum‐based process. At both scales, the agitation used during culture was the minimum required for microcarrier suspension, N_JS. The use of the ambr15, with its improved control compared to the spinner flask, reduced the coefficient of variation on viable cell density in the serum containing medium from 7.65% to 4.08%, and the switch to serum free further reduced these to 1.06–0.54%, respectively. The combination of both serum‐free and automated processing improved the reproducibility more than 10‐fold compared to the serum‐based, manual spinner flask process. The findings of this study demonstrate that the ambr15 microbioreactor is an effective tool for bioprocess development of hMSC microcarrier cultures and that a combination of serum‐free medium, control, and automation improves both process yield and consistency. Biotechnol. Bioeng. 2017;114: 2253–2266. © 2017 The Authors. Biotechnology and Bioengineering Published by Wiley Periodicals, Inc.