Cell cycle kinetics of the accumulation of heavy and light chain immunoglobulin proteins in a mouse hybridoma cell line

Rates of accumulation of immunoglobulin proteins have been determined using flow cytometry and population balance equations for exponentially growing murine hybridoma cells in the individual G₁, S and G₂+M cell cycle phases. A producer cell line that secretes monoclonal antibodies, and a nonproducer clone that synthesizes only -light chains were analyzed. The pattern for the kinetics of total intracellular antibody accumulation during the cell cycle is very similar to the previously described pattern for total protein accumulation (Kromenaker & Srienc 1991). The relative mean rate of heavy chain accumulation during the S phase was approximately half the relative mean rate of light chain accumulation during this cell cycle phase. This indicates an unbalanced synthesis of heavy and light chains that becomes most pronounced during this cell cycle phase. The nonproducer cells have on average an intracellular light chain content that is 42% lower than that of the producer cells. The nonproducer cells in the G₁ phase with low light chain content did not have a significantly higher rate of light chain accumulation relative to other G₁ phase nonproducer cells. This is in sharp contrast to what was observed for the G₁ phase producer cells. In addition, although the relative mean rate of accumulation of light chain was negative for G₂+M phase nonproducer cells, the magnitude of this relative mean rate was less than half that observed for the producer cells in this cell cycle phase. This suggests that the mechanisms that regulate the transport of fully assembled antibody molecules through the secretion pathway differ from those which regulate the secretion of free light chains. The results reported here indicate that there is a distinct pattern for the cell cycle dynamics of antibody synthesis and secretion in hybridomas. These results are consistent with a model for the dynamics of secretion which suggests that the rate of accumulation of secreted proteins will be greatest for newborn cells due to an interruption of the secretion pathway during mitosis.     

Application of population balance model to the loss of hybridoma antibody productivity.

A simple dynamic model has been applied to explain the population dynamics of monoclonal antibody (MAb) producing (producer) and nonproducing hybridoma cells (nonproducer) coexisting in culture. The events of mutation or loss of genes associated with antibody synthesis have been incorporated into the model to account for the conversion of a producer to a nonproducer. The model shows that the cell population is not necessarily dominated by the nonproducer, and a steady balance of producer and nonproducer populations can be achieved. A nonproducer population is undesirable, and cultivation strategies to maximize MAb production are suggested, taking into account the dynamics of a nonproducer population.     

Effect of temperature on hybridoma cell cycle and MAb production

The kinetics of growth and antibody formation of an anti-interleukin-2 producing hybridoma line were studied in suspension culture at temperatures ranging from 34 degrees C to 39 degrees C. Flow cytometry was used to determine the effect of temperature on the cell cycle. Maximum cell density and monoclonal antibody yield were observed at 37 degrees C. The specific monoclonal antibody production rate was approximately constant throughout each batch experiment. Lower temperatures caused cells to stay longer in the G(1)-phase of the cell cycle, but temperature had only a marginal effect on the specific antibody production rate. Arresting of cells in the G(1)-phase by means of temperature was, therefore, not suited for enhanced monoclonal antibody production. Rather, antibody production for this hybridoma was directly linked to viable cell concentration. (c) 1992 John Wiley & Sons, Inc.     

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.     

Relationship between hybridoma growth and monoclonal antibody production.

Factors affecting cell growth and antibody production in a mouse hybridoma were investigated. Antibody was produced during the growth and decline phases of a batch culture with an increase in the specific rate of antibody production during the decline phase. The specific rate of antibody production was also increased in cells arrested by 2 mM thymidine, suggesting that cell proliferation and antibody production can be uncoupled. Reduced serum concentrations resulted in lower cell growth rates but increased antibody production rates. However, this trend was reversed in hybridomas which had been arrested by thymidine, since the highest antibody production rate was associated with high serum concentrations. Likewise, in proliferating cells, the optimum pH for antibody production (pH 6.8) was lower than the optimum pH for cell growth (pH 7.2), whereas in thymidine-blocked cells, the highest antibody production rate was at pH 7.2. High antibody production rates and product yields were also associated with low growth rates in continuous cultures. The possibility that antibody was under cell cycle control was investigated in synchronized hybridoma cultures. Antibody production occurred during G1 and G2 with a decline in the M phase and evidence of a further decline in the S phase. Thus antibody production was not restricted to the G1 and S phase in this hybridoma.     

Microinjection of mRNA coding for an anti-Golgi antibody inhibits intracellular transport of a viral membrane protein

Messenger RNA was prepared from a hybridoma cell line secreting a monoclonal antibody (53FC3) directed against a luminal epitope of a Golgi membrane protein (Mr = 135 kd) found in rodent cells. When this mRNA was microinjected into the cytoplasm of BHK cells, mouse IgG was seen to accumulate in the Golgi complex after 5-6 hr of incubation. No accumulation was seen in 3T3 cells which lack the epitope recognized by 53FC3. When microinjected BHK cells were infected with vesicular stomatitis virus, surface expression of the viral G protein was considerably reduced when compared with neighboring noninjected cells.     

Growth and production kinetics of human x mouse and mouse hybridoma cells at reduced temperature and serum content.

The growth and production kinetics of a mouse hybridoma cell line and a human-mouse heterohybridoma were analyzed under conditions of reduced temperature and serum content. The mouse hybridoma P24 had a constant cell specific production rate and RNA content, while the heterohybridoma 3D6-LC4 showed growth associated production kinetics and an increased RNA content at higher growth rates. This behaviour of 3D6-LC4 cells can be explained by the unusual cell cycle kinetics of this line, which can be arrested in any phase under growth limiting conditions, so that a low growth rate does not result in a greater portion of high producing G1-phase cells. Substrate limitation changes the cell cycle distribution of this cell line to a greater extent than low temperature or serum content, which indicates that this stress factor exerts a greater physiological control than assumed.     

Cell cycle model for growth rate and death rate in continuous suspension hybridoma cultures

As a result of recent advances in flow cytometry, renewed interest is shown in modeling the kinetic behavior of cells in culture on the basis of cell cycle parameters. An important but often overlooked kinetic variable in hybridoma cultures is the cell death rate. Not only the overall cell growth but also the kinetics of nutrient metabolism and monoclonal antibody production have been shown to depend on the cell death rate in continuous suspension hybridoma cultures. The present study shows that the death rate in hybridoma cultures is proportional to the fraction of cells arrested in the G(1) phase of the cell cycle. The steady-state cell age distributions in the various phases of the division cycle have been calculated analytically. A simple mathematical model has been used to produce the profiles of the cycling and arrested cell fractions with respect to the dilution rate. The calculated steady-state growth rate, death rate, and viability profiles are shown to be in agreement with recently published experimental data from continuous suspension hybridoma cultures. (c) 1992 John Wiley & Sons, Inc.     

An unstructured kinetic model of macromolecular metabolism in batch and fed-batch cultures of hybridoma cells producing monoclonal antibody

Growth profiles of the batch and fed-batch culture of hybridoma cells producing monoclonal antibody were simulated using an unstructured model. The model describes the production of cellular macromolecules and monoclonal antibody, the metabolism of glucose and glutamine with the production of lactate and ammonia, and the profiles of cell growth in batch and fed-batch culture. Equations describing the cells arrested in G1 phase [T.I. Linardos, N. Kalogerakis, L.A. Behie, Biotechnol. Bioeng. 40 (1992) 359–368; E. Suzuki, D.F. Ollis, Biotechnol. Bioeng. 34 (1989) 1398–1402] were included in this model to describe the increase of the specific antibody productivity in the near-zero specific growth rate, which was observed in the recent experiments in fed-batch cultures of this study and the semi-continuous culture of hybridoma cells [S. Reuveny, D. Velez, L. Miller, J.D. Macmillan, J. Immnol. Methods 86 (1986) 61–69]. This model predicted the increase of specific antibody production rate and the decline of the specific production rate of cellular macromolecules such as DNA, RNA, protein, and polysaccharide in the late exponential and decline phase of batch culture and at lower specific growth rates in the fed-batch culture.     

Mechanisms and kinetics of monoclonal antibody synthesis and secretion in synchronous and asynchronous hybridoma cell cultures.

The kinetics of monoclonal antibody synthesis and secretion have been studied in synchronous and asynchronous mouse hybridoma cell cultures. Pulse-labelling of IgG followed by immunoprecipitation and quantitation of synthesized and secreted IgG in synchronous cultures show maximum production during G1/S phases. Secretion takes place through exocytotic release of vesicle contents. Pulse-chase experiments show that 71% of the synthesized IgG is secreted within 8 h of the pulsing period and only a further 4% is secreted by 22 h. Higher specific antibody production (QA) is obtained if (a) cells are arrested and then maintained in G1/S phases, (b) viability is decreased during the death phase of batch culture, (c) the dilution rate is decreased in continuous culture or (d) cells are subjected to hydrodynamically induced stress. The increase in QA in all these cases is mainly due to the passive release of the accumulated intracellular antibody. DNA and protein synthetic activity peak during the early exponential phase and decline rapidly during mid and late exponential and death phases. Metabolic activity however peaks up to 20 h after the peak in DNA synthesis, and declines similarly during the death phase. The data are consistent with the idea that slow growth and higher death rates increase QA and that Ig secretion is probably subject to complex intracellular control.     

Enhanced expression of various exogenous genes in recombinant Chinese hamster ovary cells in presence of dimethyl sulfoxide

Dimethyl sulfoxide (DMSO) (1% v/v) stimulated stable transformed Chinese hamster ovary (CHO) cells to synthesize different recombinant proteins and repress their proliferation rate. The expressions of a fusion protein and -galactosidase were increased 1.6- and 1.4-fold after adding DMSO. The expression of fusion protein was increased by up to 2.8-fold that of uninduced control by the simultaneous addition of DMSO and pentanoic acid. However, DMSO did not increase the production of the monoclonal antibody (immunoglobulin G) of three hybridoma cell lines (OKM1, OKT4 and HyGPD-YK-1-1), although it could inhibit the growth rates of the hybridoma.     

Growth, metabolic, and antibody production kinetics of hybridoma cell culture: 1. Analysis of data from controlled batch reactors.

A mouse-mouse hybridoma cell line (167.4G5.3) was cultivated in a 1.5-L stirred-tank bioreactor under constant pH and dissolved oxygen concentration. The transient kinetics of cell growth, metabolism, and antibody production were followed by biochemical and flow cytometric methods. The cell-specific kinetic parameters (growth and metabolic rates) as well as cell size were constant throughout the exponential phase. Intracellular protein and RNA content followed a similar trend. Cell growth stopped when the glutamine in the medium was depleted. Glucose could not substitute for glutamine, as glucose consumption ceased after glutamine depletion. Ammonia and lactate production followed closely glutamine and glucose consumption, respectively. Alanine, glutamate, serine, and glycine were produced but other amino acids were consumed. The cells are estimated to obtain about 45% of the total energy from glycolysis, with the balance of the metabolic energy provided by oxidative phosphorylation. The antibody was produced at a constant rate in both the exponential and decline phases of growth. The intracellular antibody content of the cells remained relatively constant during the exponential phase of growth and decreased slightly afterwards.     

Kinetics of amino acid transport by human-mouse myeloma hybrids--difference between human immunoglobulin producers and nonproducers

Somatic cell hybridization techniques have allowed the preparation of interspecies hybrids that express the features of both parental cell lines. We have studied hybrids made with human myeloma cells fused to a continuous mouse myeloma cell line. In the present study we analyzed the kinetics of leucine influx and efflux in Ig producer and nonproducer hybrids. We found no statistical difference in amino acid influx; however, the rates of efflux were markedly increased in nonproducer hybrids as compared to the producers. The producer cells were tested further in puromycin known to inhibit protein synthesis. Under these conditions amino acid influx was not altered, but efflux was markedly increased resembling the findings in nonproducers. We conclude that hybrids that synthesize human immunoglobulins show decreased efflux of labeled leucine and this effect can be abolished by inhibition of protein synthesis. This difference in the efflux rate appears to be a consequence of immunoglobulin synthesis, rather than a component of a control mechanism of Ig synthesis.     

Surface IgG content of murine hybridomas: Direct evidence for variation of antibody secretion rates during the cell cycle

Previous experiments have shown that population average surface lgG content is correlated with the specific antibody production rates of batch hybridoma cultures. Therefore, surface associated lgG content of single hybridoma cells might indicate antibody secretion rates of individual cells. Moreover, the surface lgG content should reflect the pattern of secretion rates during the cell cycle. To probe for lgG secretion rates during the cellcycle, a double staining procedure has been developed allowing simultaneousflow cytometric analysis of surface lgG content and DNA content of murine hybridoma cells. Crosslinking of the surface associated immunofluorescence with the cell by paraformaldehyde fixation permits subsequent DNA staining without loss of immunofluorescence. The optimized protocol has been used to determine the pattern of the surface lgG fluorescence as a function of the cell cycle position. It is highest during the G2+M cell cycle phase and the experimental data are in excellent agreement with the previously predicted secretion pattern during the cell cycle. (c) 1995 John Wiley & Sons Inc.     

无牛血清IgG细胞培养基（—GFCS培养基）的制备及其在杂交瘤细胞体外培养中的应用

为了制备不含牛血清IgG的细胞培养基（－GFCS培养基）,并研究其在杂交瘤细胞体外培养中的应用,采用蛋白G亲和层析的方法,将含有血清的细胞培养基中的牛血清IgG去除,以制备无IgG的培养基。使用该培养基体外培养杂交瘤细胞后,监测细胞生长和上清抗体浓度。对培养上清中的IgG类单克隆抗体可以采用蛋白G亲和层析进行纯化。与示去除牛血清IgG的培养基相比,－GFCS培养基培养的杂交瘤细胞的生长状况及上清抗体浓度均无明显变化;从－GFCS培养上清中成功纯化出不被血清IgG污染的IgG类单克隆抗体,本文结果表明,采用－GFCS培养基体外培养分泌IgG类单抗的杂交瘤细胞,可以简化上清抗体的纯化工艺。     

DMSO抑制杂交瘤增殖促进抗体的分泌

利用DMSO促进杂交瘤细胞分泌单克隆抗体,并对其作用机制进行了研究。结果表明在杂交瘤细胞对数生长后期添加0.6%浓度的DMSO与对照相比可提高抗体的产量2倍;流式细胞仪检测细胞周期表明此时837%的细胞处于G1期;免疫印记结果显示在有DMSO作用下杂交瘤细胞P27 蛋白表达显著升高。因此,DMSO 可通过促进P27蛋白的表达,抑制杂交瘤细胞的增殖,从而提高杂交瘤细胞分泌抗体的能力。对DMSO进一步在高密度大规模培养杂交瘤细胞中的应用具有重要意义。     

Biological responses of hybridoma cells to hydrodynamic shear in an agitated bioreactor.

Effects of long-term hydrodynamic shear on hybridoma cells were investigated in a 250-ml continuous stirred-tank reactor (CSTR). Cells grown at steady state were subjected to step changes in agitation rates. Cell viability, glucose consumption, and monoclonal antibody (MAb) production were determined at high agitation rates and compared with the control (100 rev min-1). Impeller tip speeds higher than 40 cm s-1 caused a significant drop in cell concentration and respiration activity, and increased lactate dehydrogenase (LDH) release to the culture medium. Also, high agitation speeds caused a decrease in MAb concentration and an increase in specific glucose consumption rate. The effects of dilution rate and serum concentration on the sensitivity of hybridoma cells to hydrodynamic shear were determined. Serum was found to protect the cells against shear damage and had a significant positive effect on hybridoma growth and MAb production. Shear damage on cells in CSTR was approximated to first-order kinetics. The death rate constant increased sharply at impeller tip speeds above 40 cm s-1.     

Regulation of the synthesis of total cellular proteins and monoclonal antibodies in a hybridoma cell culture

A study was made of the regulation of total protein synthesis in cells of the mouse hybridoma producing monoclonal antibodies (McAb) against lambda phage, and in the course of hybridoma growth and at the change of fetal bovine serum (FBS) concentration. FBS strictly affected proliferation of hybridoma cells, the specific production of McAb per cell being unchanged. The rate of total cellular protein synthesis does depend on FBS concentration in the medium, whereas the rates of protein degradation and secretion do not. Evidence is presented that the reduction in the protein-synthesis rate, after the removal of FBS from the medium, is caused by a coordinated decrease in both the rate of protein synthesis initiation and the rates of polypeptide chain elongation and translation termination. The decrease in the protein synthesis rate at the stationary phase of cell growth was shown to be related to the three main factors: 1) a 15-25% decrease in ribosome content per cell; 2) a two-fold decrease of the ribosome portion involved in mRNA translation; 3) a 5 to 15% decrease in the rate of mRNA translation. Evidence is presented that the decrease in the portion of mRNA translating ribosomes is due to the decrease in the rate of protein synthesis initiation.     

Characterization of cross-reacting antigens on the Epstein-Barr virus envelope and plasma membranes of producer cells.

A rabbit antiserum has been prepared against the B95-8 transforming strain of EBV. The antiserum has a high virus neutralizing titer (approximately 1:1000) against both the marmoset B95-8 EBV and the human P3HR-1 EBV. The neutralizing antibodies may be absorbed completely with EBV producer cell lines, but not with nonproducer cell lines or producer cell lines treated with phosphonoacetic acid (PAA) so as to be nonproducer. After repeated absorption with PAA-treated B95-8, the serum remains reactive with the membranes of producer cell lines as judged by immunofluorescence or the 125I--Staphylococcal protein A radioimmunoassay. Thus the neutralizing antigens are expressed on the membranes of producer cell lines and may be purified from this source using the serum and 125I--Staph A binding as an assay. The ability of the serum to differentiate between producer and nonproducer cells by means of cell surface determinants has been exploited to achieve a separation of these two populations from the same culture. Immunoprecipitation by the protein A technique shows that the serum recognizes two polypeptides from producer cells of approximate molecular weights 150,000 and 75,000.