Hybridoma cells in a protein-free medium within a composite gel perfusion bioreactor

A composite gel system has been developed combining the chemical and physical properties of calcium alginate and agarose gels. The results of growing composite gel immobilized hybridoma SPO1 cells in a protein-free medium within a fluidized-bed perfusion bioreactor are presented in this paper. During the continuous operation of this system, the total cell density reached 3.9×10⁷ cells per ml of beads (viability 79.6%). The specific productivity of monoclonal antibody of the immobilized hybridoma cells reached more than 1.5 g per 10⁶ viable cells per hour, compared with 0.5 for non-immobilized viable cells grown in a one liter agitated bioreactor with the same medium. Significant increases in cell metabolic activities, including substrate utilization and byproduct formation, were also observed. Leaching of materials from the beads was evident and the major fraction of released materials was alginate.     

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.     

Kinetic studies on hybridoma cells immobilized in fixed bed reactors

Cultures with immobilized hybridoma cells were performed in fixed bed systems. "Steady state" values for volume-specific substrate uptake and metabolite production rates were determined at various perfusion rates and superficial flow velocities of the medium within the carrier matrix. Data from fixed bed volumes between 50 and 600 ml did not show any difference. The volume-specific glutamine and glucose uptake rate turned out to be independent of the superficial flow velocity, but decreased with decreasing glutamine and glucose concentration. The volume-specific oxygen uptake rate increased with increasing superficial flow velocity and substrate concentration, respectively. A similar behavior was observed for the ratio between oxygen and glucose uptake rate. The production rate for monoclonal antibodies was neither affected by the substrate concentration nor by the superficial flow velocity. The metabolic parameters of the immobilized cells were put into kinetic equations and compared to those of suspended cells. It could be concluded that the metabolism of the immobilized cells is determined by the oxygen supply within the macroporous carriers. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 535-541, 1997.     

Continuous production of L-arginine using immobilized growing Serratia marcescens cells: Effectiveness of supply of oxygen gas

Summary The immobilized growing cell system using Serratia marcescens was applied to continuous L-arginine production. From the determination of oxygen uptake rate, it was shown that the cells entrapped in carrageenan gel were in an oxygen-limited state due to the diffusion barrier to oxygen transport created by the gel layer. This limited state in gel was relieved by supply of oxygen-enriched gas instead of air into the medium. The maximum population of immobilized cells increased to five times that of free cells with the supply of pure oxygen gas. The L-arginine-producing activity of the immobilized growing cells was proportional to the concentration of oxygen gas supplied and was 6 mg/h per millilitre in gel supplied with pure oxyges gas. The continuous L-arginine containing production was constantly maintained by controlling the medium penicillin G at pH 6.5 and more than 10 mg/ml of L-arginine were obtained at 10h of residence time for at least 12 days.     

A model for oxygen supply in fixed bed reactors with immobilized hybridoma cells

In fixed bed reactors with animal cells immobilized in macroporous carriers sufficient oxygen supply is a critical parameter. For modelling of the oxygen consumption and the oxygen profile in a fixed bed oxygen gradients within the porous carriers and along the length of the fixed bed have to be considered. For the complex geometry of the fixed bed a model structure was assumed, that allows the calculation of the oxygen profile. The model for oxygen supply of the immobilized cells included the transport resistance from the bulk fluid into the carriers and diffusion within the carriers. The model was compared with experimental data obtained with a hybridoma cell line for production of monoclonal antibodies. Model calculations and experimental data agree rather well. The mean volume-specific oxygen uptake rate as an indicator for the cell activity increased with the superficial flow velocity of the bulk liquid flow, and did not depend on the length of the fixed bed in the range tested. This indicates, that the convective transport from the bulk liquid flow between the carriers to the outer surface of the carriers is a dominating transport resistance besides the diffusive oxygen supply within the carriers.     

Growth kinetics of animal cells immobilized within porous support particles in a perfusion culture

The growth kinetics of anchorage-independent animal cells [mouse myeloma MPC-11 (ATCC CCL 167) immobilized within porous polyvinyl formal resin biomass support particles (BSPs; 3 × 3 × 3 mm cubes; mean pore diameter, 60 µm) was analyzed by measuring intracellular and extracellular lactate dehydrogenase (LDH) activities in a perfusion culture. First, the intracellular LDH content of cells immobilized within the BSPs was assayed in a shake-flask culture and found to remain almost comparable to that of non-immobilized cells in the exponential growth phase under static culture. Then, cells inoculated in the BSPs were grown in a continuous stirred-tank bioreactor. Using the LDH content of non-immobilized cells, the density of immobilized cells and the numbers of leaked and dead cells were evaluated, respectively, by the intracellular LDH activity of immobilized and leaked cells and the LDH activity in cell-free culture supernatant. In the initial period, immobilized cells exhibited exponential growth at a constant apparent specific growth rate; however, the acutal specific growth rate, which takes into consideration cell death and cell leakage, decreased significantly. In the stationary phase, the actual specific growth rate maintained a constant but markedly lower value than during exponential growth.     

Kinetics of phosphorus uptake by immobilizedChlorella

Summary Alginate-entrappedChlorella demonstrate rapid uptake of phosphorus from synthetic growth medium in batch culture. Rates of phosphorus uptake demonstrated by immobilized algae were found to be much lower than those of non-immobilized cells. Uptake was dependent upon matrix stocking density, cell preculture conditions and cell viability, but not upon cell growth.     

Mercury removal by immobilized algae in batch culture systems

The accumulation and volatilization of mercury by non-immobilized and immobilizedChlorella emersonii have been studied in batch culture systems. Reduction in the mercury concentration in the growth medium by non-immobilized cells was highly dependent on inoculum density, whilst reduction in mercury concentration by immobilized cells was rapid at all inoculum densities. Mercury accumulation by immobilized cell biomass was significantly greater than by non-immobilized cells with 10⁶ and 10⁵ cells bead^–1 or ml^–1. Volatilization of mercury by non-immobilized cell systems was greatest at higher inoculum densities, whereas more mercury was volatilized from immobilized cell systems at lower inoculum densities, and was greatest with unstocked alginate beads. Thus, in immobilized systems, mercury removal from solution is complex and involves mercury accumulation by the cells and volatilization by the matrix and cells. Further studies of mercury accumulation and volatilization by unstocked immobilization matrices revealed that agarose volatilized much less mercury than alginate or agar. The precise mechanism of mercury volatilization by alginate remains unclear, though it is thought to be a chemical effect.     

Continuous production of monoclonal antibody with immobilized hybridoma cells in an expanded bed fermentor

Summary Continuous production of monoclonal antibody was achieved in serum-free medium by hybridoma cells immobilized by calcium alginate. The cells were cultivated in an expanded bed fermentor under mild flow conditions which reduced destruction of the immobilized gel particles. Monoclonal antibody was produced continuously for more than 40 days.     

Oxygen uptake of microorganisms entrapped in Ca-alginate

Summary The oxygen uptake rates of Pseudomonas putida, Saccharomyces cerevisiae and Aspergillus niger, immobilized in Ca-alginate gel, were determined in comparison with the respiration of free cells. The specific oxygen uptake rate of immobilized microorganisms decreased with increasing cell content of the gel beads and increasing alginate concentration.Abbreviations ATCC American Type Culture Collection - DFA Deutsche Forschungsanstalt für Lebensmittelchemie - DSM Deutsche Stammsammlung von Mikroorganismen - DW dry weight - rpm rounds per minute     

Oxygen uptake by entrapped hybridoma cells

Oxygen consumption by hybridoma cells immobilized in 1- and 3.9-mm-diameter calcium alginate beads was measured. The entrapped cells consumed oxygen at about 10 mumol/min per 10(9) cells, regardless of the bead size and cell loading. In contrast, the same cells in suspension culture respire at specific rates of 3-8 mumol/min per 10(9) cells (depending on the cell density). The growth rate of the immobilized cells was significantly reduced, while specific antibody production was comparable to that of free cells.     

Growth and death behaviour of anchorage-independent animal cells immobilized within porous support matrices

Summary Growth and death of anchorage-independent animal cells entrapped within porous biomass support particles (BSPs) in static or shake-flask cultures were evaluated by comparison of enzyme activity with non-immobilized cells grown under static culture using 3-(4,5-dimethylthiazol-2-yl)-2,5-diphenyl tetrazolium bromide (MTT) assay and release of lactate dehydrogenase into the culture medium. Mouse myeloma MPC-11 (ATCC CCL 167) cells inoculated within porous polyvinyl formal resin BSPs (3 × 3 × 3 or 2 × 2 × 2 mm; mean pore diameter, 60 ) grew exponentially at a specific growth rate comparable to that of non-immobilized cells in the initial period of incubation. Entrapped cells then reached the stationary phase with a cell density over 10⁷ cells/cm³ BSP. The death rate of entrapped cells increased in response to the rise in viable cell density in the BSPs. Observation of viable cell distribution within the BSPs using MTT staining indicated that the cells concentrated within a thin outer shell of the BSPs with time. After the immobilized cells reached the stationary phase, penetration of cells into the outer shell ceased and heterogeneous distribution of cell density occurred in the viable cell layer in the shake-flask culture.     

New immobilization method of mammalian cells using alginate and polyacrylate

Mouse-mouse hybridoma cells were immobilized in polyacrylate-alginate gels. The immobilized hybridoma cells were cultured semi-continuously using a fluidized bed reactor, and allowed continuous antibody production without any gel destruction for one month. It has been proved that the polyacrylate-alginate gels were tolerant against physical stress. The composition of the gels suitable for cell growth and antibody production was given as follows; viscosity of alginate at 1% solution: 60–100 cP, alginate concentration: 0.8%, and polyacrylate concentration: 0.2%. In the semi-continuous culture using gels prepared under suitable conditions, the viable cell number was estimated as 2.5×10⁷ cells/ml-gel, and the antibody production rate was 2.2 mg/ml-gel/d, at maximum.     

Change in growth kinetics of hybridoma cells entrapped in collagen gel affected by alkaline supply

The growth yields for glucose and glutamine of murine hybridoma cells entrapped in collagen gel particles were examined during the growth phase. The immobilized hybridoma cells were cultivated in a fluidized bed fermenter where the medium was circulating to supply oxygen separately. Procedures to supply an alkaline solution for adjusting the pH level strongly affected the growth yields. A direct supply of the alkaline solution to the cultivation system reduced both the growth yields for glucose and glutamine, probably due to a local increase in pH level. On the other hand, when fresh medium in which the pH was adjusted to around 8.5 was added to the cultivation system, the growth yields were unchanged even at the same pH level as when direct alkaline supply was used. These results suggest that an indirect alkaline supply could be recommended to ajust the pH level when using medium-circulating-fermenters.     

Penicillin G production by immobilized whole cells of Penicillium chrysogenum.

Penicillium chrysogenum was immobilized in polyacrylamide gel prepared from 5% acrylamide monomers (85% acrylamide and 15% N,N'-methylene bisacrylamide). Penicillin produced from glucose by the immobilized mycelium was 17% of that produced by washed mycelium. However, the activity of penicillin production of the washed mycelium decreased with repeated use. On the other hand, the activity of the immobilized mycelium increased initially and decreased gradually with repeated use. The rate of oxygen uptake of the immobilized mycelium was about 30% of that of the washed mycelium. The immobilized mycelium required oxygen for the production of penicillin.     

Effects of oxygen aeration on production of monoclonal antibody in immobilized hybridoma-cell bioreactor

Continuous production of monoclonal antibody by hybridoma cells immobilized with alginate and urethane polymer was done using a fluidized bed bioreactor with direct bubbling. Increasing the dilution rate did not affect the antibody production rate under aeration with air. By changing the aeration gas to oxygen instead of air, the antibody production rate was increased 2-fold. The monoclonal antibody could be produced continuously for more than 40 d.     

Immobilization of animal cells using photo-crosslinkable resin

A photo-crosslinkable resin, BIX12, was selected from among various photo-crosslinkable resins for the immobilization of animal cells. BIX12 had no cytotoxic effect on the growth of hybridoma cells and the production of monoclonal antibody, although other photo-crosslinkable resins had significant inhibitory effects. Using BIX12-alginate hybrid gel particles, hybridoma cells could grow in the resins and produce monoclonal antibody. For the continuous production of monoclonal antibody, perfusion culture using a fluidized-bed bioreactor with direct air bubbling was carried out. By this cultivation, monoclonal antibody could be produced stably for more than 50 d. A high viable cell density of more than 10⁷ cells/ml-gel was attained, and the antibody productivity was improved 8.5-fold compared with conventional suspension culture using a spinner flask. Anchorage-dependent cells were also immobilized in the resin particles by three immobilization procedures. Among these procedures, porous BIX12 formed by adding gelatin powder provided good support strength and allowed the cells to grow on the surface inside of the support.     

Effect of pre-immobilization conditions on phosphate uptake by immobilized Chlorella

Summary Batch culture studies of phosphate uptake by non-immobilized (free) and immobilized (Ca-alginate-entrapped) Chlorella emersonii have shown that exponentially growing free cells remove phosphate from the medium five times more rapidly than cells in late stationary phase. Culture age is also shown to be an important factor in determining the uptake abilities of cells when in their immobilized state. When cells of different ages are immobilized in Ca-alginate and placed in a small-scale packed-bed reactors the effects of culture age are sufficient to produce significant differences in reactor performance lasting in the order of five days.     

Nitrogen fixation by immobilized Azotobacter chroococcum

A nitrogen-fixing bacterium, Azotobacter chroococcum, was immobilized in 2% agar gel. The optimum partial oxygen pressure, pO₂, of immobilized cells was 0.2 atm, wherea s that of native cells was 0.05 atm. When continual nitrogen fixation was performed under aerobic conditions, the nitrogenase activity of immobilized cells increased with increasing time. On the other hand, the activity of native cells decreased rapidly. Increase of nitrogenase activity was attributed to growth of the bacteria in the gel matrix. The production rate of total nitrogen compounds by the immobilized bacteria was also increased during the first 4 days. Nitrogen compounds produced by the immobilized cells were mainly amino acids such as γ-aminobutyrate, glutamate and arginine.     

Effects of cell density and glucose and glutamine levels on the respiration rates of hybridoma cells

The effects of cell density as well as the concentration levels of glucose and glutamine on the specific respiration rate of a hybridoma cell line were investigated. The experimental oxygen consumption rate was found to be constant over a wide range of dissolved oxygen levels if the suspension medium contained glutamine. In glutamine-free medium, however, the rate of oxygen consumption decreased slowly with time.In a stationary flask batch culture, the specific respiration rate decreased from about 7 to 2.9 mumol/min per 10(9) cells as the cell density increased exponentially from 1 x 10(5) to 1.2 x 10(6)/mL. To isolate the effect of cell density, cells were re suspended in fresh culture medium so that nutrient concentrations were the same for all experiments. The specific respiration rate decreased with increasing cell density in the same manner as in the stationary flask culture, falling from 8 to 4 mumol/min per 10(9) cells as the cell density increased from 10(5) to 10(6) cells/mL, then declining to 2 mumol/min per 10(9) cells when the cell density reached 10(7) cells/mL.Cells suspended in Hanks balanced sale solution (HBSS) were used to elucidate the effect of glucose and glutamine levels on respiration. The addition of glucose in concentrations of 0.25, 0.50, and 0.75 g/L had no observable effect on the specific oxygen uptake rate; however, a glucose concentration of 1 g/L reduced the uptake rate by 22%. Glutamine in a concentration of 0.30 g/L increased the specific respiration rate in HBSS containing 0 and 1 g/L glucose by approximately 13%.