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.     

Immobilization of 293 cells using porous support particles for adenovirus vector production

Adenovirus vector production by anchorage-independent 293 cells immobilized using porous biomass support particles (BSPs) was investigated in static and shake-flask cultures for efficient large-scale production of adenovirus vectors for gene therapy applications. The density of cells immobilized within BSPs was evaluated by measuring their WST-8 (2-(2-methoxy-4-nitrophenyl)-3-(4-nitrophenyl)-5-(2,4-disulfophenyl)-2H-tetrazolium, monosodium salt) reduction activity. In shake-flask culture, 293-F cells, which were adapted to serum-free suspension culture, were not successfully retained within reticulated polyvinyl formal (PVF) resin BSPs (2 × 2 × 2 mm cubes) with matrices of relatively small pores (pore diameter 60 μm). When the BSPs were coated with a cationic polymer polyethyleneimine, a high cell density of more than 10⁷ cells cm⁻³-BSP was achieved in both static and shake-flask cultures with regular replacement of the culture medium. After infection with an adenovirus vector carrying the enhanced green fluorescent protein gene (Ad EGFP), the specific Ad EGFP productivity of the immobilized cells was comparable to the maximal productivity of non-immobilized 293-F cells by maintaining favorable conditions in the culture environment.     

Long-term cultivation of anchorage-independent animal cells immobilized within reticulated biomass support particles in a circulating bed fermentor

Summary Long-term cultivation of anchorage-independent animal cells immobilized within porous biomass support particles (BSPs) using a gas-stirred circulating bed fermentor (CBF) was investigated. Inoculation of mouse myeloma MPC-11 (ATCC CCL 167) cells into reticulated polyvinyl formal resin BSPs (3 × 3 × 3 mm; mean pore diameter, 60 m; porosity, 0.88) and the repeated batch culture of inoculated cells were performed under gentle circulation of BSPs, induced by sparging air from the base of the fermentor. The glucose uptake rate of cells decreased in the initial period just after the start of circulation, since a relatively large number of cells leaked from the BSPs. After that period, the uptake rate gradually increased and the leakage of cells diminished. In the meantime, when inoculated cells were incubated statically by introducing air into the upper part of the fermentor for the initial several days before circulating the BSPs, glucose consumption became very rapid and cell density in the BSPs reached at least 10⁷ cells/cm³ BSP. Thus, a long-term cultivation without significant leakage of cells and with high cell density in BSPs was successfully achieved in the CBF-BSP system.Offprint requests to: H. Yamaji     

Culture conditions for intracellular lipase production by Rhizopus chinensis and its immobilization within biomass support particles

Acetone-dried cells of Rhizopus chinensis (with a 1,3-positional specificity lipase) were investigated for the interestierification reaction of olive oil and methyl stearate. First, the culture conditions for intracellular lipase production were examined, and then the activities of dried cells obtained from immobilization in Biomass Support Particles (BSPs) were compared with those of freely suspended cells.It was clear from cultivation of freely suspended cells that intracellular lipase activity for the interesterification reaction was enhanced sifnificantly by the presence of oleic acid, oil, and tea oil, but that the presence of glucose reduced the activity.The specific activity of dried cells within BSPs increased 7-fold compared with that obrained from freely suspended cells.The process presented here, using immobilization within BSPs, can provide cells directly as a catalyst with high activity, where cells become immobilized simply during batch operation, and no special preparation of cells is necessary. Therefore, the reaction system using dried cells immobilized within BSPs is a promising interesterifcation process for industrial applications.     

The use of lactate dehydrogenase (LDH) release kinetics for the evaluation of death and growth of mammalian cells in perfusion reactors

A general methodology is proposed to estimate the actual specific growth and death rate of mammalian cells in continuous perfusion reactors from the monitoring of the release of the cytoplasmic enzyme lactate dehydrogenase (LDH) in the culture medium. The procedure is illustrated on a perfusion culture of human tumor kidney cells growing on microcarriers and producing prourokinase (PUK). The intracellular LDH content of living attached cells is checked to be constant during the culture. However, cells detached from the microcarriers, and counted dead because of the uptake of trypan blue, have only released part of their intracellular LDH. In the culture medium, LDH is relatively stable as the loss of activity does not exceed 5% per day. The time variation of the LDH concentration in the medium is used to calculate the total amount of lysed and actually produced cells in the reactors, hence, the actual specific rates of cell growth and death. It is thus found that the stationary phase observed after 400 h of perfusion culture is the result of equal growth and death rates, with a daily renewal of living cells on the microcarriers near 10%. Moreover, for the cell line tested, the production of PUK is associated with cellular growth.     

Oxygen uptake rate of immobilized growing hybridoma cells

Summary The specific oxygen uptake rate of hybridoma cells immobilized in calcium alginate gel particles was measured, and the observed data was compared with those of non-immobilized cells. The uptake rate of the immobilized cells coincided with that of the non-immobilized hybridoma cells just after immobilization, but increased with cell growth. On the other hand, the cellular glucose consumption rate decreased slightly during the experiments. The increased oxygen uptake rate by immobilized cells was closely related to the formation of cell colonies in the gel particles.     

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.     

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.     

Growth rate control in fed-batch cultures of recombinant Saccharomyces cerevisiae producing hepatitis B surface antigen (HBsAg)

Summary A recombinant Saccharomyces cerevisiae producing hepatitis B surface antigen (HBsAg) exhibited growth-assciated product formation. By controlling the medium feed rate, based on the calculated amount of medium required for 1 h, a constant specific growth rate was obtained in the range of 1.12-0.18 h^–1. In order to prolong the exponential growth phase, the medium feed rate was increased exponentially. A fedbatch cultivation method based on the production kinetics of batch culture enhanced HBsAg production ten times more than in batch culture. The reason for the increase can be explained by the fact that the production of HBsAg is expressed as an exponential function of time when the specific growth rate is controlled to a constant value in growth-associated product fromation kinetics. In the scale-up of this culture to 91, the specific growth rate could also be maintained constant and the HBsAg production trend was similar to that in a 1-l culture. However, ethanol accumulation occurred at a late stage in fed-bach culture. Ethanol produced was not reutilized and inhibited further cell growth. Offprint requests to: M. B. Gu     

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.     

Cell cycle kinetics and monoclonal antibody productivity of hybridoma cells during perfusion culture

The flow-cytometric (FCM) analysis of bivariate DNA/lgG distributions has been conducted to study the cell cycle kinetics and monoclonal antibody (MAb) production during perfusion culture of hybridoma cells. Three different perfusion rates were employed to demonstrate the dependency of MAb synthesis and secretion on cell cycle and growth rate. The results showed that, during the rapid growth period of perfusion culture, the level of intracellular igG contents of hybridoma cells changed significantly at each perfusion rate, while the DNA histograms showing cell cycle phases were almost constant. Meanwhile, during the reduced growth period of perfusion culture, the fraction of cells in the S phase decreased, and the fraction cells in the G1/G0 phase increased with decreasing growth rate. The fraction of cells in the G2/M phase was relatively constant during the whole period of perfusion culture. Positive correlation was found between mean intracellular IgG contents and the specific MAb production rate, suggesting that the deletion of intracellular IgG contents by a flow cytometer could be used as a good indicator for the prediction of changes in specific MAb productivity following manipulation of the culture condition. (c) 1994 John Wiley & Sons, Inc.     

Strategies to extend longevity of hybridomas in culture and promote yield of monoclonal antibodies

Summary Cell viability was improved by supplemental feeding of amino acids and vitamins in batch culture of hybridoma cells. Cells could be maintained over a 10 day period following exponential growth at a constant viable cell concentration of 2.1×10⁶ cells/ml. Concentrations of monoclonal antibody (MAb) reached 140 mg/l, a value of nearly four times that found in typical batch culture. Lactate formation appeared to occur only during active exponential growth and not during the stationary phase.     

Production of monoclonal antibody using free-suspended and immobilized hybridoma cells: Effect of serum

The effect of serum on cell growth and monoclonal antibody (MAb) productivity was studied in a repeated fedbatch mode using both free-suspended and immobilized S3H5/gamma2bA2 hybridoma cells. In the suspension culture, serum influenced the cell growth rate but not the specific MAb productivity. The average specific growth rate of the suspension culture in medium containing 10% serum was approximately 0.99 +/- 0.12 day(-1) (+/-standard deviation), while that in medium containing 1% serum was approximately 0.73 +/- 0.12 day(-1). The specific MAb productivity was almost constant at 3.69 +/- 0.57 mug/10(6) cells/day irrespective of serum concentration reached a maximum at ca. 1.8 x 10(6) cells/mL of medium in 10% serum medium, and the cell concentration was gradually reduced to 1%. The specific MAb productivity of the immobilized cells was more than three times higher than that of the free-suspended cells. The amount of serum in the medium did not influence the specific MAb production rate of the immobilized cells. The maintenance of high cell concentration and the enhanced specific MAb productivity of the immobilized cell culture resulted in a higher volumetric MAb productivity. In addition, MAb yield in the immobilized cell culture with medium containing 1% serum was 2.2 mg/mL of serum, which was approximately three times higher than that in the suspension culture.     

Growth rate control in fed-batch cultures of recombinant Saccharomyces cerevisiae producing hepatitis B surface antigen (HBsAg).

A recombinant Saccharomyces cerevisiae producing hepatitis B surface antigen (HBsAg) exhibited growth-associated product formation. By controlling the medium feed rate, based on the calculated amount of medium required for 1 h, a constant specific growth rate was obtained in the range of 0.12-0.18 h-1. In order to prolong the exponential growth phase, the medium feed rate was increased exponentially. A fed-batch cultivation method based on the production kinetics of batch culture enhanced HBsAg production ten times more than in batch culture. The reason for the increase can be explained by the fact that the production of HBsAg is expressed as an exponential function of time when the specific growth rate is controlled to a constant value in growth-associated product formation kinetics. In the scale-up of this culture to 91, the specific growth rate could also be maintained constant and the HBsAg production trend was similar to that in a 1-1 culture. However, ethanol accumulation occurred at a late stage in fed-bach culture. Ethanol produced was not reutilized and inhibited further cell growth.     

Analysis of cell cycle activity and population dynamics in heterogeneous plant cell suspensions using flow cytometry

Flow cytometry was used to measure cell cycle parameters in Solanum aviculare plant cell suspensions. Methods for bromodeoxyuridine (BrdU) labeling of plant nuclei were developed so that cell cycle times and the proportion of cells participating in growth could be determined as a function of culture time and conditions. The percentage of cells active in the cell cycle at 25 degrees C decreased from 52% to 19% within 7.6 d of culture; presence of a relatively large proportion of non-active cells was reflected in the results for culture growth. While the maximum specific growth rate of the suspensions at 25 degrees C was 0.34 d-1 (doubling time: 2.0 d), the specific growth rate of active cells was significantly greater at 0.67 d-1, corresponding to a cell cycle time of 1.0 d. A simple model of culture growth based on exponential and linear growth kinetics and the assumption of constant cell cycle time was found to predict with reasonable accuracy the proportion of active cells in the population as a function of time. Reducing the temperature to 17 degrees C lowered the culture growth rate but prolonged the exponential growth phase compared with 25 degrees C; the percentage of cells participating in the cell cycle was also higher. Exposure of plant cells to different agitation intensities in shake flasks had a pronounced effect on the distribution of cells within the cell cycle. The proportion of cells in S phase was 1.8 times higher at a shaker speed of 160 rpm than at 100 rpm, while the frequency of G0 + G1 cells decreased by up to 27%. Because of the significant levels of intraculture heterogeneity in suspended plant cell systems, flow cytometry is of particular value in characterizing culture properties and behavior.     

Effects of high cell density on growth-associated monoclonal antibody production by hybridoma T0405 cells immobilized in macroporous cellulose carriers

Relationship between monoclonal antibody (MAb) productivity and growth rate, and effects of high cell density on MAb production of hybridoma T0405 cells immobilized in macroporous cellulose carriers were investigated in continuous and batch cultures. The results showing, that the specific MAb production rate increased with increasing specific growth rate in both suspended and immobilized continuous cultures indicate a positively growth-associated relationship between MAb productivity and growth rate. Moreover, the specific production rate was higher in the immobilized cell culture than that in suspended one at all dilution rates. In order to clarify these phenomena, MAb mRNA expression and cell cycle distribution were investigated in batch cultures with immobilized cells and suspended cells. RT-PCR was used for observation of MAb mRNA expression and a two-color bromode-oxyuridine (BrdU)/propidium iodide (PI) flow cytometry method for determination of cell cycle distribution. The results revealed that MAb mRNA expression reached the peak during the exponential growth phase, suggest a positively growth-associated MAb production. And the immobilized cells continued the MAb mRNA expression until dead phase, which was longer than that in suspended cells. The cell cycle distribution patterns were observed almost the same for both immobilized and suspended cells. Such results may imply that a high cell density state has positive influence on the mRNA expression and on growth-associated MAb productivity of T0405 cells.     

Fermentation kinetics of free and immobilized Penicillium raistrickii able perform the 15α-hydroxylation of 13-ethyl-gon-4-ene-3,17-dione

Growing Penicillium raistrickii i 477 cells immobilized by microencapsulation, entrapment in calcium alginate beads and photopolymerization were used for the 15α-hydroxylation of 13-ethyl-gon-4-en-3,17-dione (I) to 15α-hydroxy-13-ethyl-gon-4-en-3,17-dione (II). The immobilized cells had lower maximum specific growth rates and yield coefficients when cultivated on the carbon source glucose than the non-immobilized cells, which leads to lower volumetric productivities than the use of nonimmobilized cells. However, the cells immobilized by microencapsulation and calcium alginate entrapment showed a specific productivity equal to that of the respective non-immobilized cells based on product formation per dry biomass and time. Photommobilized cells were not able to grow in the presence of the steroid because the substrate concentrations within the polymer reached inhibiting amounts for growth and product formation. In the absence of the steroid, the growing photoimmobilized cells showed a prolonged lag-phase in comparison with the free cells.     

Determination of antibody content in live versus dead hybridoma cells: analysis of antibody production in osmotically stressed cultures

Hybridomas are known to exhibit increased specific antibody production rated when subjected to environmental stress. Under these conditions, viability is low so that population-average measurements do not properly reflect the state of viable cells. Even for flow cytometry, which gives a population distribution, special techniques must be used to discriminate between viable and nonviable cells. We describe the use of the vital stain ethidium monoazide (EMA) for independent measurement of intracellular antibody content in live and dead cells via flow cytometry. EMA is shown to be superior to light scattering techniques in identifying dead cells. We apply this technique to show that, in control batch culture, the specific antibody prodution rate and antibody content in live cells are constant during exponential growth, but decrease as cells enter the stationary phase. Antibody is retained in dead cells, but at a lower level than in live cells. We further show that, under hyperosmotic stress, the specific antibody production rate and antibody content in live both remain high during death phase. (c) 1992 John Wiley & Sons, Inc.     

CHOLINE METABOLISM AND MEMBRANE FORMATION IN RAT HEPATOMA CELLS GROWN IN SUSPENSION CULTURE : II. Phosphatidylcholine Synthesis during Growth Cycle and Fluctuation of Mitochondrial Density

The incorporation of methyl-labeled choline into phosphorylcholine and phosphatidylcholine of cellular membranes by Novikoff rat hepatoma cells (line N1S1-67) during growth in suspension culture was investigated. Upon initiation of a fresh culture at 10⁵ cells/ml, the rate of synthesis of phosphorylcholine by the cells was four to five times greater than that of the synthesis of phosphatidylcholine. While the rate of synthesis of the latter remained relatively constant, the rate of phosphorylation of choline decreased progressively during the course of the growth cycle of the culture to 10–20% of the initial rate when the culture reached stationary phase at 3 x 10⁶ cells/ml. The decrease in phosphorylcholine synthesis during the growth cycle was not due to depletion of choline in the medium or a decrease in its concentration, but was correlated with a decrease in choline kinase activity of the cells as measured in cell-free extracts. Newly synthesized phosphatidylcholine was detectable in cells only as an integral part of cellular membranes. Its distribution among various cytoplasmic membrane structures separated by isopycnic centrifugation in sucrose density gradients remained relatively constant during the growth cycle. About 50% was associated with the mitochondria, and the remainder with plasma membrane fragments and other membranous structures with mean densities of about 1.15 and 1.13 g/cm³, respectively. However, the density of the mitochondria increased from about 1.167 g/cm³ in early exponential phase cells to about 1.190 g/cm³ in stationary phase cells. The finding that the density of the entire propulation of mitochondria changed simultaneously and progressively is in agreement with the view that mitochondria grow by addition of phospholipids and structural proteins and increase in number by division.     

Kinetic analysis of hybridoma cells viability under mechanical shear stress with and without serum protection

The effect of a well-defined mild shear stress on hybridoma cell viability (HB-8852) in a serum-free culture medium has been analysed, and the role as shear protector of different concentrations of fetal bovine serum have been studied. Samples harvested from cultures in their late exponential growth phase, were subjected in a rheometer to a constant shear stress of 0.41 ± 0.02 Pa, and the evolution of viable and total cell concentrations was determined and compared with static controls. A simple segregated kinetic model for the viable and dead cells was used to know the effect of serum concentration on the specific cell growth and death rate of the cells.