Enhanced cell culture performance using inducible anti-apoptotic genes E1B-19K and Aven in the production of a monoclonal antibody with Chinese hamster ovary cells

Mammalian cells are used for the production of numerous biologics including monoclonal antibodies. Unfortunately, mammalian cells can lose viability at later stages in the cell culture process. In this study, the effects of expressing the anti-apoptosis genes, E1B-19K and Aven, separately and in combination on cell growth, survival, and monoclonal antibody (MAb) production were investigated for a commercial Chinese Hamster Ovary (CHO) mammalian cell line. CHO cells were observed to undergo apoptosis following a model insult, glucose deprivation, and at later stages of batch cell culture. The CHO cell line was then genetically modified to express the anti-apoptotic proteins E1B-19K and/or Aven using an ecdysone-inducible expression system. Stable transfected pools induced to express Aven or E1B-19K alone were found to survive 1-2 days longer than the parent cell line following glucose deprivation while the expression of both genes in concert increased cell survival by 3 days. In spinner flask batch studies, a clonal isolate engineered to express both anti-apoptosis genes exhibited a longer operating lifetime and higher final MAb titer as a result of higher viable cell densities and viabilities. Interestingly, survival was increased in the absence of an inducer, most likely as a result of leaky expression of the anti-apoptosis genes confirmed in subsequent PCR studies. In fed-batch bioreactors, the expression of both anti-apoptosis genes resulted in higher growth rates and cell densities in the exponential phase and significantly higher viable cell densities, viabilities, and extended survival during the post-exponential phase. As a result, the integral of viable cells (IVC) was between 40 and 100% higher for cell lines engineered to express both Aven and E1B-19K in concert, and the operational lifetime of the fed-batch bioreactors was increased from 2 to 5 days. The maximum titers of MAb were also increased by 40-55% for bioreactors containing cells expressing Aven and E1B-19K. These increases in volumetric productivity arose primarily from enhancements in viable cell density over the course of the fed-batch culture period since the specific productivities for the cells expressing anti-apoptosis genes were comparable or slightly lower than the parental hosts. These results demonstrate that expression of anti-apoptosis genes can enhance culture performance and increase MAb titers for mammalian CHO cell cultures especially under conditions such as extended fed-batch bioreactor operation.     

Fed-batch culture of recombinant NS0 myeloma cells with high monoclonal antibody production

An amplified NS0 cell line transfected with a vector expressing a humanized monoclonal antibody (MAb) against CD-18 and glutamine synthetase (GS) was cultivated in a 1.5 L fed-batch culture using a serum-free, glutamine-free medium. Concentrated solutions of key nutrient components were fed periodically using a simple feeding control strategy. Feeding amounts were adjusted daily based on the integral of viable cell concentration over time (IVC) and assumed constant specific nutrient consumption rates or yields to maintain concentrations of the key nutrient components around their initial levels. On-line oxygen uptake rate (OUR) measurement was used to aid empirically the adjustment of the feeding time points and amounts by inferring time points of nutrient depletion. Through effective nutritional control, both cell growth phase and culture lifetime were prolonged significantly, resulting in a maximal viable cell concentration of 6.6 x 10(9) cells/L and a final IVC of 1.6 x 10(12) cells-h/L at 672 h. The final MAb concentration reached more than 2.7 g/L. In this fed-batch culture, cellular metabolism shifts were repeatedly observed. Accompanying the culture phase transition from the exponential growth to the stationary phase, lactate, which was produced in the exponential growth phase, became consumed. The time point at which this metabolism shift occurred corresponded to that of rapid decrease of OUR, which most likely was caused by nutrient depletion. This transition coincided with the onset of ammonia, glutamate and glutamine accumulation. With removal of the nutrient depletion by increasing the daily nutrient feeding amount, OUR recovered and viable cell concentration increased, while cell metabolism shifted again. Instead of consumption, lactate became produced again. These results suggest close relationships among nutrient depletion, cell metabolism transition, and cell death. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 783-792, 1997.     

Fed-batch culture optimization of a growth-associated hybridoma cell line in chemically defined protein-free media

An investigation was made to study the processes of fed-batch cultures of a hybridoma cell line in chemically defined protein-free media. First of all, a strong growth-associated pattern was correlated between the production of MAb and growth of cells through the kinetic studies of batch cultures, suggesting the potential effectiveness of extending the duration of exponential growth in the improvement of MAb titers. Second, compositions of amino acids in the feeding solution were balanced stepwisely according to their stoichiometrical correlations with glucose uptake in batch and fed-batch cultures. Moreover, a limiting factor screening revealed the constitutive nature of Ca²⁺ and Mg²⁺ for cell growth, and the importance of their feeding in fed-batch cultures. Finally, a fed-batch process was executed with a glucose uptake coupled feeding of balanced amino acids together with groups of nutrients and a feeding of CaCl₂ and MgCl₂ concentrate. The duration of exponential cell growth was extended from 70 h in batch culture and 98 h in fed-batch culture without Ca²⁺/Mg²⁺ feeding to 117 h with Ca²⁺/Mg²⁺ feeding. As a result of the prolonged exponential cell growth, the viable and total cell densities reached 7.04 × 10⁶ and 9.12 × 10⁶ cells ml⁻¹, respectively. The maximal MAb concentration achieved was increased to approximately eight times of that in serum supplemented batch culture.     

Control of culture environment for improved polyethylenimine-mediated transient production of recombinant monoclonal antibodies by CHO cells

In this study we describe optimization of polyethylenimine (PEI)-mediated transient production of recombinant protein by CHO cells by facile manipulation of a chemically defined culture environment to limit accumulation of nonproductive cell biomass, increase the duration of recombinant protein production from transfected plasmid DNA, and increase cell-specific production. The optimal conditions for transient transfection of suspension-adapted CHO cells using branched, 25 kDa PEI as a gene delivery vehicle were experimentally determined by production of secreted alkaline phosphatase reporter in static cultures and recombinant IgG4 monoclonal antibody (Mab) production in agitated shake flask cultures to be a DNA concentration of 1.25 microg 10(6) cells(-1) mL(-1) at a PEI nitrogen:DNA phosphate ratio of 20:1. These conditions represented the optimal compromise between PEI cytotoxicity and product yield with most efficient recombinant DNA utilization. Separately, both addition of recombinant insulin-like growth factor (LR3-IGF) and a reduction in culture temperature to 32 degrees C were found to increase product titer 2- and 3-fold, respectively. However, mild hypothermia and LR3-IGF acted synergistically to increase product titer 11-fold. Although increased product titer in the presence of LR3-IGF alone was solely a consequence of increased culture duration, a reduction in culture temperature post-transfection increased both the integral of viable cell concentration (IVC) and cell-specific Mab production rate. For cultures maintained at 32 degrees C in the presence of LR3-IGF, IVC and qMab were increased 4- and 2.5-fold, respectively. To further increase product yield from transfected DNA, the duration of transgene expression in cell populations maintained at 32 degrees C in the presence of LR3-IGF was doubled by periodic resuspension of transfected cells in fresh media, leading to a 3-fold increase in accumulated Mab titer from approximately 13 to approximately 39 mg L(-1). Under these conditions, Mab glycosylation at Asn297 remained essentially constant and similar to that of the same Mab produced by stably transfected GS-CHO cells. From these data we suggest that the efficiency of transient production processes (protein output per rDNA input) can be significantly improved using a combination of mild hypothermia and growth factor(s) to yield an extended "activated hypothermic synthesis".     

Fed-batch bioreactor performance and cell line stability evaluation of the artificial chromosome expression technology expressing an IgG1 in Chinese hamster ovary cells

The artificial chromosome expression (ACE) technology system uses an engineered artificial chromosome containing multiple site-specific recombination acceptor sites for the rapid and efficient construction of stable cell lines. The construction of Chinese hamster ovary(CHO) cell lines expressing an IgG1 monoclonal antibody (MAb) using the ACE system has been previously described (Kennard et al., Biotechnol Bioeng. 2009;104:540-553). To further demonstrate the manufacturing feasibility of the ACE system, four CHO cell lines expressing the human IgG1 MAb 4A1 were evaluated in batch and fed-batch shake flasks and in a 2-L fed-batch bioreactor. The batch shake flasks achieved titers between 0.7 and 1.1 g/L, whereas the fed-batch shake flask process improved titers to 2.5–3.0 g/L. The lead 4A1 ACE cell line achieved titers of 4.0 g/L with an average specific productivity of 40 pg/(cell day) when cultured in a non optimized 2-L fed-batch bioreactor using a completely chemically defined process. Generational stability characterization of the lead 4A1-expressing cell line demonstrated that the cell line was stable for up to 75 days in culture. Product quality attributes of the 4A1 MAb produced by the ACE system during the stability evaluation period were unchanged and also comparable to existing expression technologies such as the CHO-dhfr system. The results of this evaluation demonstrate that a clonal, stable MAb-expressing CHO cell line can be produced using ACE technology that performs competitively using a chemically defined fed-batch bioreactor process with comparable product quality attributes to cell lines generated by existing technologies.     

Stability of antibody productivity is improved when hybridoma cells are entrapped in calcium alginate beads

Loss of monoclonal antibody (MAb) productivity in long-term, free-suspended cell culture is often attributed to the appearance of a nonproducing population of hybridoma cell (NP) in the culture which has a growth advantage over the producing population (P). However, when an NP appears in long-term culture of entrapped cells, it may not be able to take over the whole culture in a short period of time due to the limited growth of the entrapped cells. In order to examine the hypothesis that entrapped cells can have improved stability of MAb productivity due to limited cell growth, free-suspended cell culture and calcium alginate-entrapped cell culture with inocula consisting of a P and an NP were compared with regard to stability of MAb productivity in a repeated fed-batch culture. In free-suspended cell culture, the NP appeared to take over the whole culture within three batches, and thereby MAb production completely disappeared. In entrapped cell culture, an NP appeared to outgrow the P rapidly only during an exponential growth phase, resulting in a significant decrease in specific MAb productivity, q(MAb), from 11.58 mug/10(6) cell/day to 2.76 mug/10(6) cell/day. However, when the cell growth was limited in entrapped cell culture, the NP no longer outgrew the P rapidly, as indicated by the stable value of q(MAb). In addition, when the cells recovered from the alginate beads by citrate buffer treatment were subcultured in free-suspended cell culture, MAb production rapidly deteriorated and completely disappeared within two batches. Thus, the P present at a small fraction of viable cell concentration in the beginning of the free-suspended cell culture, which were previously entrapped in alginate beads, seemed to be outgrown rapidly by the NP. Taken together, the results obtained from these experiments support the hypothesis that the limited cell growth in entrapped cell culture, which keeps an NP from taking over the whole culture, is responsible, in part, for the improved stability of MAb productivity. (c) 1993 John Wiley & Sons, Inc.     

Repeated fed-batch culture of hybridoma cells in nutrient-fortified high-density medium

Long-term high-density cultivation of the hybridoma 2c3.1 was successfully carried out in a repeated fed-batch mode using high-density media that were constructed to meet in vitro cell growth limitations. The high-density culture was possible in a range of 0.5 approximately 1.0 x 10(7) cells/mL in MBRI 40-02 medium for over 2500 h by the repeated supplementation of the most fortified medium, MBRI 40-03, and consequently, distinct enhancement of MAb production was achieved. MAb concentrations were maintained around 1 g/L for about 1000 h of the process and the maximum MAb concentration was around 1.56 g/L. The result supported strongly the fact that the nutritional fortification was the most critical factor for high-density cell culture in vitro. The mean chromosome number of the hybridoma 2c3.1 was maintained stably for about 1500 h, whereas gradual loss of the MAb activity was apparent during the long-term cultivation. (c) 1993 John Wiley & Sons, Inc.     

中国仓鼠卵巢工程细胞无血清流加培养关键工艺参数的考察

主要考察流加培养基中不同营养成分、流加起始时间及初始接种密度对11G-S细胞无血清流加培养的影响。在研究中以悬浮适应的表达尿激酶原 (Pro-urokinase,Pro-UK) CHO工程细胞系11G-S为研究对象,在100 mL的摇瓶中无血清悬浮流加培养11G-S细胞,同时以活细胞密度、细胞活力及Pro-UK活性为评价依据。结果表明在培养基中氨基酸、无血清添加成分及无机盐对促进细胞生长、细胞活力维持及蛋白表达起着较为重要的作用;且流加起始时间为72 h及初始接种密度为3×105~4×105 cells/     

Continuous culture of RPMI 8226 human cells

Continuous culture of RPMI 8226 human hematopoietic cells was performed. The viable cell number and glucose, lactate and ammonium concentrations became constant within 3–4 days at a constant dilution rate. The viable cell number decreased at low and high dilution rates. The growth and product yields slightly depended on the dilution rate, except for product yield for lactate based on cell number. Growth characteristics of these cells at various dilution rates could be expressed by equations considering the maintenance energy in growth yield. Maximum specific growth rate could be evaluated from the wash-out profile and the known inhibition constants.     

Low-glutamine fed-batch cultures of 293-HEK serum-free suspension cells for adenovirus production

Recent developments in gene therapy using adenoviral (Ad) vectors have fueled renewed interest in the 293 human embryonic kidney cell line traditionally used to produce these vectors. Low-glutamine fed-batch cultures of serum-free, suspension cells in a 5-L bioreactor were conducted. Our aim was to tighten the control on glutamine metabolism and hence reduce ammonia and lactate accumulation. Online direct measurement of glutamine was effected via a continuous cell-exclusion system that allows for aseptic, cell-free sampling of the culture broth. A feedback control algorithm was used to maintain the glutamine concentration at a level as low as 0.1 mM with a concentrated glucose-free feed medium. This was tested in two media: a commercial formulation (SFM II) and a chemically defined DMEM/F12 formulation. The fed-batch and batch cultures were started at the same glucose concentration, and it was not controlled at any point in the fed-batch cultures. In all cases, fed-batch cultures with double the cell density and extended viable culture time compared to the batch cultures were achieved. An infection study on the high density fed-batch culture using adenovirus-green fluorescent protein (Ad-GFP) construct was also done to ascertain the production capacity of the culture. Virus titers from the infected fed-batch culture showed that there is an approximately 10-fold improvement over a batch infection culture. The results have shown that the control of glutamine at low levels in cultures is sufficient to yield significant improvements in both cell densities and viral production. The applicability of this fed-batch system to cultures in different media and also infected cultures suggests its potential for application to generic mammalian cell cultures.     

High-level production of a monoclonal antibody in murine myeloma cells by perfusion culture using a gravity settler

A perfusion system is described for the production of a human monoclonal antibody in non-secreting murine myeloma (NS0) cells that was previously shown to be difficult to produce at high levels using fed-batch culture. The perfusion system was based on the use of a commercially available cell settler as the separation device to separate the cells from the culture. Separation efficiency of the cell settler was above 98%. Based on the growth and glucose consumption rates, fresh media was added to the culture and the turnover rate for the bioreactor was set at a maximum of 1.5 times the bioreactor volume per day. The perfusion process resulted in twice the maximum viable cell densities and up to three times the total protein production in a 53-day run period when compared to the fed-batch process. In addition, charge heterogeneity of the antibody as measured by ion exchange chromatography was lower for material purified from the perfusion runs compared to fed-batch. Perfusion mode of culture using a commercially available gravity settler is therefore a viable alternative to fed-batch mode for high-level production of this monoclonal antibody in NS0 cells.     

Heterogeneous conditions in dissolved oxygen affect N-glycosylation but not productivity of a monoclonal antibody in hybridoma cultures

It is known that heterogeneous conditions exist in large-scale animal cell cultures. However, little is known about how heterogeneities affect cells, productivities, and product quality. To study the effect of non-constant dissolved oxygen tension (DOT), hybridomas were subjected to sinusoidal DOT oscillations in a one-compartment scale-down simulator. Oscillations were forced by manipulating the inlet oxygen partial pressure through a feedback control algorithm in a 220-mL bioreactor maintained at a constant agitation. Such temporal DOT oscillations simulate spatial DOT gradients that can occur in large scales. Different oscillation periods, in the range of 800 to 12,800 s (axis of 7% (air saturation) and amplitude of 7%), were tested and compared to constant DOT (10%) control cultures. Oscillating DOT decreased maximum cell concentrations, cell growth rates, and viability indexes. Cultures at oscillating DOT had an increased glycolytic metabolism that was evidenced by a decrease in yield of cells on glucose and an increase in lactate yield. DOT gradients, even several orders of magnitude higher than those expected under practical large-scale conditions, did not significantly affect the maximum concentration of an IgG(1) monoclonal antibody (MAb). The glycosylation profile of the MAb produced at a constant DOT of 10% was similar to that reported in the literature. However, MAb produced under oscillating culture conditions had a higher amount of triantennary and sialylated glycans, which can interfere with effector functions of the antibody. It was shown that transient excursions of hybridomas to limiting DOT, as occurs in deficiently mixed large-scale bioreactors, is important to culture performance as the oscillation period, and thus the time cells spent at low DOT, affected cell growth, metabolism, and the glycosylation pattern of MAb. Such results underline the importance of monitoring protein characteristics for the development of large-scale processes.     

An immobilized hybridoma culture perfusion system for production of monoclonal antibodies

A fixed bed perfusion system for hybridoma cell immobilization is presented. The system consists of a culturing vessel (300 ml total volume) in which polyurethane (PU) sponges in the form of small cubes of about 5 mm sides are packed. Cells are immobilized by physical entrapment in the foam matrix. By entrapment of the cells in the pores of the matrix high cell concentration can be maintained in a mechanically protected environment. Medium is continuously circulated by an airlift pump mounted in the cell-free chamber (700 ml total volume).Medium flow rate, feeding rate, dissolved oxygen, pH, nutrient uptake and waste product formation can be easily monitored and controlled. Steady state conditions are established with medium dilution rates of 1.0–1.5 reactor volume per day. The steady state is characterized by a constant cell density, constant culture volume and constant glucose and lactate levels. Cell-free supernatant is collected continuously in a cold room adjacent to the 37°C culture room. Monoclonal antibodies (MAb) are produced at a concentration of 150–200 g/ml for several weeks. An important feature of the system is the capacity to maintain a population of cells after the growth phase in a non-proliferating state for extended time periods expressing high titers of MAb.Abbreviations DO Dissolved Oxygen - FBS Fetal Bovine Serum - FBR Fixed Bed Reactor - MAb Monoclonal Antibody - PU polyurethane     

High cell density and high monoclonal antibody production through medium design and rational control in a bioreactor

A simple feeding strategy was developed and successfully employed for nutritional control in a 2-L fed-batch culture of hybridoma cells. A previously developed stoichiometric model for animal cell growth was used to design a supplemental medium for feeding. Undialyzed fetal bovine serum and trace metals (Fe(2+), SeO(3) (2-), Li(+), Zn(2+), and Cu(2+)) were fed to the cells periodically in addition to the automatic feeding of other nutrients in the supplemental medium. In this study, the maximum viable cell density was increased from 6.3 x 10(6) to 1.7 x 10(7) cells/mL, and the culture span was extended from 340 to 550 hours. The final monoclonal antibody titer achieved was 2400 mg/L. The specific production rates for ammonia and lactate were further reduced from 0.0045 and 0.0048 in our previous fed-batch experiments to 0.0028 and 0.0036 mmol/10(9) cell h, respectively. Only 3.4% of the total glucose consumption was converted into lactate, compared to 67% in a conventional batch culture.     

Metabolic and kinetic studies of hybridomas in exponentially fed-batch cultures using T-flasks

Exponentially fed-batch cultures (EFBC) of a murine hybridoma in T-flasks were explored as a simple alternative experimental tool to chemostats for the study of metabolism, growth and monoclonal antibody (MAb) production kinetics. EFBC were operated in the variable volume mode using an exponentially increasing and predetermined stepwise feeding profile of fresh complete medium. The dynamic and steady-state behaviors of the EFBC coincided with those reported for chemostats at dilution rates below the maximum growth rate. In particular, steady-state for growth rate and concentration of viable cells, glucose, and lactate was attained at different dilution rates between 0.005 and 0.05 h^–1. For such a range, the glucose and lactate metabolic quotients and the steady-state glucose concentration increased, whereas total MAb, volumetric, and specific MAb production rates decreased 65-, 6-, and 3-fold, respectively, with increasing dilution rates. The lactate from glucose yield remained relatively constant for dilution rates up to 0.03 h^–1, where it started to decrease. In contrast, viability remained above 80% at high dilution rates but rapidly decreased at dilution rates below 0.02 h^–1. No true washout occurred during operation above the maximum growth, as concluded from the constant viable cell number. However, growth rate decreased to as low as 0.01 h^–1, suggesting the requirement of a minimum cell density, and concomitant autocrine growth factors, for growth. Chemostat operation drawbacks were avoided by EFBC in T-flasks. Namely, simple and stable operation was obtained at dilution rates ranging from very low to above the maximum growth rate. Furthermore, simultaneous operation of multiple experiments in reduced size was possible, minimizing start-up time, media and equipment costs.Abbreviations EFBC exponentially-fed batch culture - CSC continuous suspended culture - MAb monoclonal antibody - D dilution rate - q _i metabolic quotient or specific rate of consumption or production of i     

Characterization of a unique glycoprotein antigen expressed on the surface of human neuroblastoma cells

In order to develop a molecular probe to delineate chemical and biological characteristics of human neuroblastoma cells, a murine monoclonal antibody (Mab 5G3) was produced that is directed to a glycoprotein, preferentially expressed on the surface of such cells. This antibody is of IgG2a isotype, has an association constant of 8 X 10(9) M-1, and reacts preferentially with human neuroblastoma cell lines and fresh frozen tissue sections in enzyme-linked immunosorbent assay and immunoperoxidase assays, respectively. Minimal reactivity is observed with a variety of lymphoblastoid cell lines and normal fetal and adult tissues. Mab 5G3 specifically recognizes a neuroblastoma target glycoprotein antigen of 215 kDa that is derived from a 200-kDa precursor, as evident from pulse-chase biosynthetic studies. Treatment with tunicamycin revealed that both molecules contain N-asparagine-linked oligosaccharides; however, only the 215-kDa species is resistant to treatment with endo-beta-N-acetylglucosaminidase H and sensitive to neuraminidase, indicating that it contains trimmed and terminally sialylated oligosaccharides of the "complex" type. In contrast, the 200-kDa precursor is sensitive to endo-beta-N-acetylglucosaminidase H and resistant to neuraminidase treatment indicating that it contains high-mannose non-processed oligosaccharides. The 215-kDa molecule is sulfated, phosphorylated at serine residues, and expressed on the cell surface. A molecule of 200 kDa is detected by Mab 5G3 in spent culture medium of human neuroblastoma cells which is neither sulfated nor phosphorylated.     

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.     

Effect of amino acid supplement on cell yield and gene product in Escherichia coli harboring plasmid

Escherichia coli harboring a recombinant plasmid was cultivated in fed-batch culture to enhance production of a gene product. Expression of the leucine gene from Thermus thermophilus in the recombinant plasmid was examined by the assay of beta-isopropylmalate dehydrogenase activity at 75 degrees C. When E. coli was cultivated in medium without leucine, biomass concentration reached 15 g/L and the specific activity became 0.082 U/mg protein. When leucine was fed in the medium throughout cultivation, although biomass concentration reached 63 g/L, the specific activity decreased to 0.016 U/mg protein. When E. coli was cultivated in medium containing 1 g leucine/L, the specific activity remained virtually constant (about 0.13 U/mg protein) and biomass concentration reached 32 g dry cells/L. In these cultivations, growth yields of several amino acids and glucose were examined. When leucine was not added to the medium, growth yields except for histidine were lowest. When leucine was fed throughout the cultivation, growth yields of glucose and tryptophan were highest. The pH-stat was useful for feeding amino acids.     

Preparation of monoclonal antibodies to nuclear DNA of mammalian cells by immunization with group A streptococcal polysaccharide conjugated with synthetic polyelectrolytes

Monoclonal antibodies (MAb) were obtained by hybridization of spleen cells from BALB/c mice immunized with streptococcal group A polysaccharide (A-PS) conjugated with synthetic polyelectrolytes (PEL). These MAb reacted with nuclei from human and mouse cells. MAb reacting with nuclei were obtained after prolonged immunization with conjugates and were not formed by hybridization of spleen cells from non-immunized mice or by the immunization with PEL. The investigation of Mab (B1/2 and A5/2) reacting with nuclei has shown that these Mab are directed against DNA and do not react with other tissue substances. No cross-reactions of Mab with A-PS used for immunization have been revealed. Mab B1/2 and A5/2 belong to autoantibodies.