| PATENT ASSIGNEE'S COUNTRY | USA |
| UPDATE | 04.00 |
| PATENT NUMBER | This data is not available for free |
| PATENT GRANT DATE | 11.04.00 |
| PATENT TITLE |
Cell culture medium for enhanced cell growth, culture longevity, and product expression |
| PATENT ABSTRACT |
Protein-free cell culture media supplements are described consisting of synergistic combinations of medium components, which when added to cell culture media, either serum supplemented or serum-free, enhance cell growth, culture longevity and product expression. |
| PATENT INVENTORS | This data is not available for free |
| PATENT ASSIGNEE | This data is not available for free |
| PATENT FILE DATE | 07.06.95 |
| PATENT REFERENCES CITED |
Bettger et al, Proc. Natl. Acad. Sci. USA, vol. 78, No. 9, pp. 5588-5592, 1981. Ill et al, In Vitro Cell & Dev. Biol., vol. 24, No. 5, pp. 413-419, May 1988. Kovar et al., "Serum-free Medium For Hybridoma And Parental Mueloma Cell Cultivation: A Novel Composition Of Growth-Supporting Substances", Immunol. Letters 7:339-345 (1984). Luan et al., "Strategies to Extend Longevity of Hybridomas in Culture and Promote Yield of Monoclonal Angtodies", Biotechnol. Letters 9:691-696 (1987). Murakami et al., "Growth of hybridoma cells in serum-free medium: Ethanolamine is an essential component", Proc. Natl. Acad. Sci. (USA) 79:1158-1162 (1982). Murakami, H., "Serum-Free Media Used for Cultivation of Hybridomas", in Monoclonal Antibodies: Production and Application 107-141 (Alan R. Liss, Inc. 1989). Murakami et al., "Development of a Basal Medium for Serum-Free Cultivation of Hybridoma Cells in High Density", Nippon Nogeikagaku Kaishi 58:575-583 (1984). Murakami et al., "Development of a basal medium for serum-free cultivation of hybridoma cells in high density", Chem. Abst. 101:71010t (1984). European Search Report (EP-B-0 435 911). Notice of Opposition to a European Patent (EP-B-0 435 911). English translation of Murakami et al., "Development of a Basal Medium for Serum-Free Cultivation of Hybridoma Cells in High Density", Nippon Nogeikagaku Kaishi 58:575-583 (1984) (14 pages; translated by Okada & Sellin Translations). Another English translation of Murakami et al., "Development of a Basal Medium for Serum-Free Cultivation of Hybridoma Cells in High Density", Nippon Nogeikagaku Kaishi 58:575-583 (1984) (18 pages). |
| PATENT PARENT CASE TEXT | This data is not available for free |
| PATENT CLAIMS |
We claim: 1. A method of growing cells, comprising the step of contacting said cells with a cell culture medium comprising the following components: (a) a first reagent selected from the group consisting of glutamine, glutamate, and asparagine, said first reagent being present at a concentration of at least 8 mM; (b) phospholipid precursors comprising at least choline and ethanolamine; (c) tryptophan; and (d) an amino acid other than tryptophan and other than said first reagent of (a); and wherein said components are at concentrations effective to increase culture longevity and product expression by maintaining said cells in a pseudo-stationary growth phase for about 100 hours or longer. 2. A method of growing cells, comprising the step of contacting said cells with a cell culture medium comprising: ______________________________________ Component Concentration (mg/L) ______________________________________ Ca(NO.sub.3).sub.2.4H.sub.2 O 40-50 KCl 400-560 MgSO.sub.4 [73.5] 73.26-242.8 NaCl [5,300] 4300-6,000 NaH.sub.2 PO.sub.4.H.sub.2 O 625-[732] 830 Na.sub.2 HPO.sub.4 [320.4] 190.66-400.5 Glucose [2,700] 1000-[4,800] 5250 Glutathione 0.4-0.5 HEPES 2383.2-2979 Sodium pyruvate 44-1155 NaHCO.sub.3 2350-2850 p-Aminobenzoate 0.464-1[.0] Biotin 0.1-0.2 Calcium pantothenate [0.170] 1.7-4.0 Folic acid 1.6[0]-[4.0] 5 Nicotinamide 2[.0]-5[.0] Pyridoxine hydrochloride 0.48-[1.0] 4 Riboflavin 0.256-0.6 Thiamine hydrochloride 2.016-5[.0] Vitamin B12 0.0025-0.24 Choline chloride 22.8-[23.5] 75 Inositol [24.9] 24.88-[41.0] 50 Ethanolamine 0.8-[10.0] 20 [Glycerol] [0-200] Glutamine 1160-[1180] 5844 PLURONIC .RTM. polyol F68 1000 [Transferrin] [4.0-5.0] [Na.sub.2 SeO.sub.3 ] [.004-.005] [FeCl.sub.3 ] [0-1.6] [(NH.sub.4).sub.6 Mo.sub.7 O.sub.24.4H.sub.2 O] [0-0.1] CoCl.sub.2.6H.sub.2 O .005-[0.1] 0.4 [CuCl.sub.2.2H.sub.2 O] [0-0.1] MnCl.sub.2.4H.sub.2 O .002-[0.1] 0.4 [ZnCl.sub.2 ] [0-0.1] [FeSO.sub.4.7H.sub.2 O] [0-0.11] [Monothioglycerol] [0-10] [Citrate] [0-258] Arginine 194.1-794 [Aspartate] Asparagine 125-[280] 1400 [Cystine] [49-195] Glutamic acid 50-308 Glycine 38-[56] 250 Histidine 45.2-[120] 300 Isoleucine 145.2-[282] 1000 Leucine 95.2-[282] 1200 Lysine hydrochloride 153.7-[317] 1000 Methionine 52-[217.6] 400 Phenylalanine 70-[232] 400 Proline 50-108 Serine 52.4-[136] 400 Threonine 72.2-[194] 500 Tryptophan 19-[140] 250 Tyrosine 66.4-[158] 500 Valine 97-[191] 600 ______________________________________ 3. A method of growing cells, comprising the step of contacting said cells with a cell culture medium comprising the following components: (a) a first reagent selected from the group consisting of glutamine, glutamate, and asparagine, said first reagent being present at a concentration of at least 8 mM; (b) phospholipid precursors comprising at least choline and ethanolamine; (c) tryptophan; and (d) an amino acid other than tryptophan and other than said first reagent of (a); and wherein said components are at concentrations effective to increase product expression of said cells to about 470 mg per liter or more of final desired protein product yield at the end of cell culture. 4. A method of growing cells, comprising the step of contacting said cells with a cell culture medium comprising the following components at the concentration set forth: ______________________________________ Component Concentration (mg/L) ______________________________________ Choline chloride >22.8 Ethanolamine >0.8 Glutamine >1160 Tryptophan >19 ______________________________________ and at least one amino acid selected from the group consisting of the following amino acids at the concentrations set forth: ______________________________________ Amino Acid Concentration (mg/L) ______________________________________ Arginine .gtoreq.194.1 Asparagine .gtoreq.125 Aspartate .gtoreq.0 Cystine or cysteine .gtoreq.0 Glutamic acid .gtoreq.50 Glycine .gtoreq.38 Histidine .gtoreq.45.2 Isoleucine .gtoreq.145.2 Leucine .gtoreq.95.2 Lysine hydrochloride .gtoreq.153.7 Methionine .gtoreq.52 Phenylalanine .gtoreq.70 Proline .gtoreq.50 Serine .gtoreq.52.4 Threonine .gtoreq.72.2 Tyrosine .gtoreq.66.4 Valine .gtoreq.97 ______________________________________ 5. The method of claim 3 or 4 wherein the cell culture medium further comprises a Class I Reagent selected from the group consisting of the following components: (i) a reducing reagent; (ii) a metal ion; (iii) a metal chelator; and (iv) a vitamin. 6. The method of claim 3 wherein the desired protein product is an antibody. 7. The method according to claim 1, further comprising contacting said cells with a growth hormone or a growth factor. 8. The method according to claim 1 further comprising contacting said cells with a Pluronic.RTM. polyol. 9. The method according to claim 1, wherein said cells are antibody secreting cells. 10. The method according to claim 1, wherein choline is present at a concentration between about 4 mg/L and 75 mg/L. 11. The method according to claim 1, wherein ethanolamine is present at a concentration between about 1 mg/L and 20 mg/L. 12. The method according to claim 1, wherein said phospholipid precursors further comprise a composition selected from the group consisting of serine, inositol, glycerol, phosphoethanolamine, phosphocholine, phosphatidylethanolamine, and phosphatidylcholine. 13. The method according to claim 12, wherein said composition is selected from the group consisting of serine, inositol, and glycerol. 14. The method according to claim 1, wherein said product expression is about 470 mg/L or more of final protein product yield at the end of cell culture. 15. The method according to claim 1, wherein said pseudo-stationary growth phase is maintained for about 150 hours or more. 16. The method according to claim 1 wherein said cells in culture are in a protein-free medium. 17. The method according to claim 1, wherein said cells in culture are in a serum-free medium. 18. The method of claim 1 wherein the cell culture medium further comprises a Class I Reagent selected from the group consisting of the following components: (i) a reducing reagent; (ii) a metal ion; (iii) a metal chelator; and (iv) a vitamin. 19. The method according to claim 18, wherein said metal ion is selected from the group consisting of calcium, magnesium, molybdenum, cobalt, copper, manganese, zinc, selenium, iron and combinations thereof. 20. The method according to claim 18 or 19, further comprising an amino acid selected from the group consisting of at least about 194 mg/L arginine, at least about 125 mg/L aspartate, at least about 49 mg/L cystine, at least about 38 mg/L glycine, at least about 50 mg/L glutamate, at least about 45.2 mg/L histidine, at least about 145.2 mg/L isoleucine, at least about 95.2 mg/L leucine, at least about 153.7 mg/L lysine, at least about 52 mg/L methionine, at least about 70 mg/L phenylalanine, at least about 50 mg/L proline, at least about 52.4 mg/L serine, at least about 72.2 mg/L threonine, at least about 19 mg/L tryptophan, at least about 66.4 mg/L tyrosine, and at least about 97 mg/L valine. 21. The method according to claim 18, wherein said reducing agent is monothioglycerol. 22. The method according to claim 21, wherein said reducing agent is included at a concentration between about 0.1 mg/L and 100 mg/L. 23. The method according to claim 18, wherein said metal chelator is selected from the group consisting of transferrin, ferritin, albumin, pyridoxyl isonicotinoyl hydrazone, choline citrate, and citrate. 24. The method according to claim 23, wherein said metal chelator is citrate. 25. The method according to claim 18, wherein said vitamin is selected from the group consisting of ascorbic acid, biotin, flavin adenine dinucleotide, folic acid, folinic acid, nicotinamide, p-amino-benzoic acid, pantothenate, pyridoxine, riboflavin, thiamine, vitamin B12 and combinations thereof. 26. A kit for prolonging the pseudo-stationary growth phase of cells grown in culture, comprising: (a) a first reagent selected from the group consisting of glutamine, glutamate, and asparagine, said first reagent providing a concentration of at least 5 mM; (b) phospholipid precursors comprising at least choline and ethanolamine; (c) tryptophan; and (d) an essential amino acid for growth of said cells other than tryptophan and other than said first reagent of (a); and wherein said components are at concentrations effective to increase culture longevity and product expression by maintaining said cells in a pseudo-stationary growth phase for about 100 hours or longer. 27. The kit according to claim 26, wherein the concentration of glutamine or glutamate is between 8 and 20 mM. 28. The kit according to claim 26 or 27, wherein the concentration of choline is between 4 and 75 mg/L. 29. The kit according to claim 26, wherein the concentration of ethanolamine is between 1 and 20 mg/L. 30. The kit according to claim 26 further comprising Class I reagents, wherein said Class I reagents comprise: (a) a reducing agent; (b) a metal ion; (c) a metal chelator; and (d) a vitamin; and further wherein said Class I reagents are at concentrations effective to maintain said cells for a prolonged time in a pseudo-stationary growth phase. 31. The kit according to claim 30, wherein said metal ion is selected from the group consisting of calcium, cobalt, copper, iron, magnesium, manganese, molybdenum, selenium and zinc. 32. The kit according to claim 30, further comprising an amino acid selected from the group consisting of at least about 426 mg/L arginine, at least about 75 mg/L aspartate, at least about 147 mg/L cystine, at least about 60 mg/L glycine, at least about 30 mg/L glutamate, at least about 84 mg/L histidine, at least about 234 mg/L isoleucine, at least about 234 mg/L leucine, at least about 279 mg/L lysine, at least about 66 mg/L methionine, at least about 120 mg/L phenylalanine, at least about 30 mg/L proline, at least about 108 mg/L serine, at least about 174 mg/L threonine, at least about 30 mg/L tryptophan, at least about 138 mg/L tyrosine, and at least about 171 mg/L valine. 33. The kit according to claim 30, wherein said reducing agent is monothioglycerol. 34. The kit according to claim 30, wherein said metal chelator is selected from the group consisting of transferrin, ferritin, albumin, pyridoxyl isonicotinoyl hydrazone, choline citrate, and citrate. 35. The kit according to claim 30, wherein said vitamin is selected from the group consisting of ascorbic acid, biotin, flavin adenine dinucleotide, folic acid, folinic acid, nicotinamide, p-amino-benzoic acid, pantothenate, pyridoxine, riboflavin, thiamine, and vitamin B12. 36. A method of growing cells, comprising the step of contacting said cells with a cell culture medium comprising: ______________________________________ Component Concentration (mg/L) ______________________________________ Ca(NO.sub.3).sub.2.4H.sub.2 O 35-55 KCl 350-600 MgSO.sub.4 70-250 NaCl 3700-6100 NaH.sub.2 PO.sub.4.H.sub.2 O 600-900 Na.sub.2 HPO.sub.4 180-450 Glucose 900-5300 Glutathione 0.3-0.6 HEPES 2300-2990 Sodium pyruvate 40-1120 NaHCO.sub.3 2340-2900 p-Aminobenzoate 0.40-1.50 Biotin 0.05-0.3 Calcium pantothenate 1.50-4.50 Folic acid 1.0-5.5 Nicotinamide 1.5-6.0 Pyridoxine hydrochloride 0.4-4.5 Riboflavin 0.20-0.70 Thiamine hydrochloride 2.4-5.5 Vitamin B12 0.0020-0.30 Choline chloride 10-80 Inositol 23-55 Ethanolamine 0.7-25 Glutamine 1160-6700 Pluronic .RTM. polyol F68 800-1200 (NH.sub.4).sub.6 Mo.sub.7 O.sub.24.4H.sub.2 O 0.003-0.5 CoCl.sub.2.6H.sub.2 O 0.005-0.5 CuCl.sub.2.2H.sub.2 O 0.01-0.5 MnCl.sub.2.4H.sub.2 O 0.01-0.5 ZnCl.sub.2 0.003-0.5 Monothioglycerol 0.7-12 Citrate 1-300 Arginine 190-1420 Glutamic acid 45-350 Glycine 30-300 Histidine 50-350 Isoleucine 1040-1050 Leucine 150-1250 Lysine hydrochloride 145-1050 Methionine 50-450 Phenylalanine 65-450 Proline 45-150 Serine 50-450 Threonine 70-600 Tryptophan 18-320 Tyrosine 60-550 Valine 90-650 ______________________________________ 37. The method according to claim 18, 19, 23, 25 2, 36, 1 or 3, wherein said first reagent is glutamine and further wherein said glutamine is present at a concentration between about 8 mM and 40 mM. 38. The method according to claim 18, 19, 23, 25, 2, 36, 1, 3 or 4, wherein said cells are hybridomas. 39. The method according to claim 18, 19, 23, 25, 2, 36, 1, 4 or 4, wherein said cells are human cells. -------------------------------------------------------------------------------- |
| PATENT DESCRIPTION |
FIELD OF THE INVENTION This invention is in the general field of animal cell culture. More particularly, the invention concerns improved media for the cultivation of animal cells and the production of natural and recombinant products derived therefrom. BACKGROUND OF THE INVENTION To date, efforts have been undertaken to develop culture conditions to maximize cell culture growth and thereby increase resultant product yield. Early work in the development of animal cell culture media focused on the formulation of such media to achieve rapid cell proliferation (White, P. R., 1946, Growth, 10:231-289, and Waymouth, C., 1974, J. Natl. Cancer Inst., 53:1443-1448). Such media incorporate specific nutrients especially sugars, amino acids, vitamins, salts, and in some cases trace metal ions, purines, and pyrimidines. These media are most often supplemented with animal serum. Today some of the more widely used basal media for mammalian cell cultures include Hams F-12, Dulbecco's modified Eagle's medium (DME), RPMI 1640, and Iscove's modified DME. Production of human monoclonal antibodies using hybridoma cell lines will be used in this application as an example for product expression in cell culture. Culture media have been previously described which were developed specifically for low serum and serum-free mammalian cell cultures for production of monoclonal antibodies. One such serum-free medium is disclosed in European Patent Publication 076,647, published Apr. 13, 1983. Other media have been developed by changing levels of supplements such as trace elements, and vitamins and incorporating purified protein hormone additives. References to such media include, for example, Barnes, D., et al., 1980 Cell, 22:649-655; Cleveland, W. L., et al., 1983, J. Immunol. Meth., 56:221-234; Iscove, N., et al., 1978, J. Exp. Med., 147:923-933; Kawamoto, T., et al., 1983, Analytical Biochemistry, 130:445-453; Kovar, J., et al., 1986, Immunology Letters, 7:339-345; Murakami, H., et al., 1983, Argic. Biol. Chem., 47(8):1835-1840; Murakami, H., et al., 1982, Proc. Natl. Acad. Sci. USA, 79:1158-1162; Muzik, H., et al., 1982, In Vitro, 18:515-524; and Wolpe, S. D., "In Vitro Immunization and Growth of Hybridomas in Serum-Free Medium", in J. P. Mather, ed., Mammalian Cell Culture, Plenum Press, New York, 1984; Hagiwara, H., et al., 1985, 117-122 in H. Murakami et al. (eds) Growth and Differentiation of Cells in Defined Environment, Springer-Verlag, Berlin, 1985; Tharakan, J. P., et al., 1986, J. Immunol. Meth., 94:225-235; Cole, S.P.C., 1987, J. Immunol. Meth., 97:29-35; McHugh, Y. E., 1983, BioTechniques, June/July issue:72-77. Components which are common to most if not all these media include glucose at concentrations up to 4.5 g/L, glutamine at concentrations of 2-4 mM, choline generally at about 1-4 mg/L, tryptophan and other amino acids. Tryptophan is generally present at concentrations less than 20 mg/L. Several of these media also contain the growth factors insulin and transferrin. Efforts to increase antibody yield have focused primarily on means to optimize cell growth and cell density. As a general point of reference, antibody titres from murine hybridoma cell lines are highly variable from cell line to cell line and range typically from 10 to 350 mg/L (Lambert, K. J., et al., 1987, Dev. Indust. Microbiol, 27:101-106). Human monoclonal antibody expression from human/human or human/mouse fusions are also highly variable from cell line to cell line and range typically from 0.1 to 25 mg/L (Hubbard, R., Topics in Enzyme and Fermentation Biotechnology, Chapt. 7:196-263, Wisemand, A., ed., John Wiley & Sons, New York (1983). These values are indicative of culture conditions that are optimized for cell growth. Another approach from the literature to increasing product production is to achieve high cell densities by cell recycle or entrapment methods. Examples of these methods include hollow fiber reactors (Altshuler, G. L., et al., 1986, Biotech. Bioeng., XXVIII:646-658; ceramic matrix reactors (Marcipar, A., et al., 1983, Annals. N.Y. Acad. Sci., 413:416-420; Nature, 302:629-630); perfusion reactors (Feder, J., et al., 1985, American Biotech. Laboratory, III:24-36) and others. While a variety of methods to increase product expression from cell culture are being explored, the primary focus is still on the optimization of cell growth. In typical culture media the culture dies rapidly after maximum cell density is reached. Another example form the literature documents that, at least for some cell lines, product (monoclonal antibody) production proceeds even after a culture stops growing (Velez, D., et al., 1986, J. Immunol. Meth., 86:45-52; Reuveny, S., et al., 1986, ibid at 53-59). Arathoon, W., et al., 1986, Science, 232:1390-1395 reported that a 1,000 liter hybridoma fermentation produced about 80 grams of monoclonal antibody during the growth phase and another 170 grams of antibody during an extended stationary/death phase. J. Birth, et al., (European Patent Application No. 87/00195, 1987) describe a procedure of Fed-batch culture wherein nutrients are added to a culture over time and culture longevity is increased. Final antibody titres from the culture are thus increased. Thus, it will be appreciated that there is a critical need for media that will support the growth of animal cells and stimulate the production of products, including antibodies, and other natural or recombinant protein products to greater levels than can be realized using media that are currently available. SUMMARY OF THE INVENTION Accordingly, the invention presented herein describes a protein-free supplement (the "Primary Supplement"), which when added to standard cell culture media, enhances cell growth, culture longevity and product expression. Examples are given showing that this supplement is particularly effective in production of antibodies using hybridoma cell lines in serum-free culture, where final antibody titre is increased in one example from 80 mg/L to over 250 mg/L. The Primary Supplement is a hitherto unrecognized synergistic combination of standard medium components which are beneficial when added in the prescribed combination, and consists of 1) glutamine, 2) phospholipid precursors, including minimally both choline and ethanolamine, 3) tryptophan, and 4) additional amino acids as required for a particular cell line and product to be produced. When added individually, to standard media, these components have little effect, but are extremely effective when added together in the prescribed combination, and the deletion of any of the prescribed components diminishes the desired effect. Several of the components in the Primary Supplement are added to concentrations hitherto considered to be unnecessary or inhibitory. When added together in the prescribed combination, the supplement enhances cell growth, increases culture longevity by maintaining cells in a pseudo-stationary phase wherein product expression continues, and thus results in a significant increase in final product titre. A second aspect of the invention is a description of several additional components, (the "Class I reagents"), which when added individually, or in various combinations to the Primary Supplement result in a further improvement to culture growth and/or product expression. Included in this class of additional components are reducing agents, trace metal ions, and/or vitamins. A third aspect of the invention is the formulation of protein-free, serum-free and serum supplemented media containing the supplement, as well as in media supplemented with lipids and can be used with the addition of agents to induce solute stress. A further aspect of the invention is a method of growing cells employing the media supplements described herein such that they can be included in medium at the start of culture, or can be added in a fed-batch or in a continuous manner. The resulting media can be used in various cultivation methods including, but not limited to, batch, fed-batch, chemostat and perfusion, and with various cell culture hardware including, but not limited to, stationary flasks, agitated flasks, spinner flasks, stirred fermentors, airlift fermentors, membrane reactors (including hollow fiber, flat membrane plate, external loop perfusion), reactor s with cells retained on a solid support or immobilized/entrapped as in microporous beads, and any other configuration appropriate for the growth or maintenance of the desired cell line. BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 shows the growth properties and levels of antibody produced by D234 in a typical commercially available medium, Ventrex HL-1. FIG. 2 shows the growth properties and levels of antibody produced by D234 in a standard serum free medium composition representative of compositions described in the cell culture literature . FIG. 3 shows the growth properties and levels of antibody produced by D234 in media supplemented with reagents of the Primary Supplement. FIG. 4 shows the growth properties and levels of antibody produced by D234 in media supplemented with reagents of the Primary Supplement and a Class I reagent. FIG. 5 shows the growth properties and levels of antibody produced by D234 in media supplemented with reagents of the Primary and Class I Supplement and used in combination with lipid supplementation. FIG. 6 shows the hybridoma D234 grown in Fed-batch with media supplemented with reagents of the Primary and Class I Supplements and lipids. Figure 7 shows the effects of growing T88 in fed-batch mode using the formulations of Table III, columns 1 and 2. FIG. 8 shows the growth properties and levels of antibody produced by the hybridoma T88-151 in DM30 media supplemented with reagents of the Primary and Class I Supplements. Note that the media used in this experiment is devoid of insulin, selenous acid and transferrin and contains high levels of iron and citrate. FIG. 9 shows the growth properties and levels of antibody produced by the hybridoma FB2, using the media of FIG. 8, but additionally containing insulin, selenous acid and transferrin. FIG. 10 shows the growth properties and levels of antibody produced by the hybridoma T88-151 in DM40. DETAILED DESCRIPTION OF THE INVENTION The following reference is referred to throughout this application, and is presented here for the convenience of the reader. Ian Freshney (Culture of Animal Cells--A Manual of Basic Technique, Alan R. Liss, NY, 1987) tabulates compositions of typical basal media for use with serum (Table 7.5:74-75) and typical serum-free media compositions (Table 7.6:76-78) described in the literature for culture of a wide range of animal cells and expression of products therefrom. These tables are incorporated by reference. The invention described herein is first concerned with a protein-free supplement compatible with standard cell culture media to enhance cell growth, culture longevity and product expression. The Primary Supplement is favored, and has advantages that arise, at least in part, by a hitherto unrecognized synergistic interaction of the reagents employed. Iscove (N. N. Iscove, Culture of Lymphocytes and Hemopoietic Cells in Serum-Free Medium:169-185 in Methods for Serum-Free Culture of Neuronal and Lymphoid Cells) describes the standard method for optimizing cell culture media wherein "the effect of individually doubling and quadrupling the concentration of each component was examined . . . ". This approach has been widely used in the cell culture field, which fails to recognize the possibility that components may act synergistically and that it may be necessary to combine supplements of several components to see a desired effect. Components selected from a second group of cell culture reagents (the Class I reagents) when combined with the Primary Supplement can synergize to produce a more favorable cell culture supplement having especially beneficial effects on cells grown to high densities. Before a detailed description of the classes of reagents is presented, and the media supplements that can be formulated therefrom, a brief definition of some of the technical terms used throughout this application will facilitate understanding the nature of the invention. I. Definitions "Basal medium" is defined herein to include a nutrient mixture of inorganic salts, sugars, amino acids, and, optionally, vitamins, organic acids and/or buffers or other well known cell culture nutrients. These reagents are necessary to support cell growth and reproduction. The preferred basal media which is a component of the instant cell growth media compositions contains neither serum, nor proteins. A wide variety of commercially available basal media are well known to those skilled in the art, and include Dulbeccos' Modified Eagles Medium (DMEM), Roswell Park Memorial Institute Medium (RPMI), Iscove modified Dulbeccos' medium and Hams medium. The amino acid concentration (in mg/L) of Dulbecco's Modified Eagle's Medium (DMEM) is: L-Arginine.HCl=84; L-Cysteine.2HCl=62.57; L-Glutamine=584; Glycine=30; L-Histidine.HCl.H.sub.2 O=42; L-Isoleucine=104.8; L-Leucine=104.8; L-Lysine.HCl=146.2; L-Methionine=30; L-Phenyalanine=66; L-Serine=42; L-Threonine=95.2; L-Trptophan=16; and L-Tyrosine disodium salt.H.sub.2 O=103.8. The amino acid concentration (in mg/L) of Roswell Park Memorial Institute Medium (RPMI) 1640 medium is L-Arginine=200; L-Asparagine.H2O=56.82; L-Aspartic acid=20; L-Cysteine.2HCl=65.2; L-Glutamic acid=20; L-Glutamine=300; Glutathione=1; Glycine=10; L-Histidine=15; L-Hydroxyproline=20 L-Isoleucine=50; L-Leucine=50; L-Lysine.HCl=40; L-Methionine=15; L-Phenylalanine=15; L-Proline=20; L-Serine=30; L-Threonine=20; L-Trptophan=5; L-Tyrosine disodium salt.H.sub.2 O=28.83; and L-Valine=20. The term "hybridoma", refers to a hybrid cell line produced by the fusion of an immortal cell line of immunologic origin, and an antibody producing cell. The term is meant to include progeny of heterohybrid myeloma fusions, which are the result of a fusion with human cells and a murine myeloma cell line subsequently fused with a plasma cell, referred to in the art as a trioma cell line. Additionally, the term is meant to encompass virtually any immortalized hybrid cell line which produced antibody such as, for example, quadromas. Milstein, C., et al., 1983, Nature, 537:3053. Moreover, the hybrid cell lines can be of virtually any species, including human and mouse. The term "microemulsion" refers to a lipid mixture emulsified substantially without the aid of proteinaceous materials such as those found in serum, particularly serum albumin. Generally, emulsifiers described in U.S. patent application Ser. No. 077,189 will be employed to form the microemulsion. This patent application is hereby incorporated by reference in its entirety. Generally, pluronic polyols are favored as the emulsifier. As used herein the phrase "solute stress" refers to the addition of solutes in such concentrations that produce a growth inhibitory effect or reduced final cell density, that is, a growth rate or maximum cell density less than that determined for optimal growth. However, the level of product expressed at this reduced growth level is comparatively greater than that level of expression achieved at the optimal growth rate owing to an increase in specific (per cell) product expression rate or an increase in longevity of the culture. Generally, solutes and methods described in U.S. patent application, Ser. No. 122,015 will be employed. This application is hereby incorporated by reference in its entirety. "Pseudo-Stationary phase" refers to a period of culture growth occurring after the exponential growth phase and wherein the rates of cell growth and death are similar such that the viable cell concentration changes only relatively slowly with time (as compared to during the exponential growth or the death phase). "Cell growth hormones" or "growth factors" is meant to encompass a large number of molecules either naturally occurring or genetically engineered, as well as fragments, derivatives or modifications thereof, that stimulate the growth, or supports the maintenance of cells in defined media. Examples of the former includes transferrin and insulin, among others. Examples of growth factors includes nerve growth factor, epidermal growth factor, fibroblast growth factor, and endothelial cell growth factor, among others. It is important to note that different animal cell lines may vary in their requirements for one or more of these molecules, and that the optimal hormones or growth factors, or a mixture of the same, is readily determined using standard cell culture techniques. As used herein the phrase "Fed-Batch" defines a method of supplying the compositions of the instant invention to cells such that the concentration of a reagent is additive of the individual additions of the reagent. The instant invention presents cell culture media supplements that are compatible with the general growth and maintenance requirements of animal (especially mammalian) cells in vitro, and particularly enhances or supports the expression of differentiated properties associated with specific cell types, for example, an elevated production of monoclonal antibodies by hybridoma cell lines. Thus, it will be appreciated that the instant supplements have widespread applications, being generally useful for routine culture of cells, as well as being employed in those instances when great amounts of a natural or recombinant cellular product is desired that is produced by cells in culture. II. Primary Supplement The Primary Supplement of the current invention consist of a class of reagents that includes, in combination, 1) glutamine, 2) phospholipid precursors including preferably choline and ethanolamine, 3) tryptophan, and 4) additional amino acids as required for the particular cells lines. A. Glutamine In the Primary Supplement, glutamine is included at over 5 mM, and preferably at 8-20 mM. However, in Fed-Batch mode glutamine may be as high as 40 mM. It is important to note that these concentrations are significantly above those typically found in cell culture media. Glutamine is recognized as both an amino acid building block for protein synthesis and as a primary energy source in cell culture (W. L. McKeehan, Glycolysis, Glutaminolysis and Cell Proliferation, Cell Biology Intro. Reports, 1982, 6(7):635-650, L. J. Reitzer, et al, Evidence that Glutamine, Not Sugar, Is the Major Energy Source for Cultured HeLa Cells, J. Biological Chemistry, 1979, 254(B):2669-2676, H. R. Zielke, et al., Reciprocal Regulation of Glucose and Glutamine Utilization by Cultured Human Diploid Fibroblasts, J. Cell Physiol., 1978, 95:41-48. Reference to the summary of typical media compositions tabulated in Freshney, above, shows that glutamine is typically included at 2 or 4 mM in standard serum-supplemented and serum-free medium formulations. In contrast, as mentioned above, the composition of the instant invention contains elevated amounts of glutamine above 5 mM, and preferably about 8-20 mM. Both glutamine metabolism as well as spontaneous decomposition of glutamine (G. L. Trisch, et al., Spontaneous Decomposition of Glutamine in Cell Culture Media, Experimental Cell Research, 1962, 28:360-364) result in the release of ammonium ion which is widely described in the literature as toxic to either cell growth or protein production (S. Reuveny, et al., Factors Affecting Cell Growth and Monoclonal Antibody Production in Stirred Reactors, J. Immunl. Methods, 1986, 86:53-59, and some researchers have argued that glutamine when added at high concentrations will have a toxic effect (indirectly through increased production of ammonium ion). Some researchers have advocated minimizing the concentration of glutamine present in the culture by adapting the culture to grow in the absence of glutamine and with glutamic acid as an alternate substrate (J. B. Griffiths, et al., The Uptake of Amino Acids by Mouse Cells During Growth in Batch Culture and Hemostat Culture, The Influence of Cell Growth Rate, Proc. Roy Soc. B., 1967, 168:421-438), or by utilizing slow addition of glutamine throughout the time course of the culture to maintain a relatively constant low concentration of glutamine (M. W. Glacken, et al., Reduction of Waste Product Excretion via Nutrient Control: Possible Strategies for Maximizing Product and Cell Yields on Serum in Cultures of Mammalian Cells, Biotechnol. Bioeng., 1986, 28:1376-1389). Based on the forgoing discussion, it will be realized that for cell lines which have been adapted to grow with glutamate or asparagine or other substitute for glutamine, that the methods of the current invention are still applicable, except that elevated levels of glutamate or other substitute would be included in the supplement in place of glutamine. For cell lines that have been adapted to grow with low concentrations of glutamine maintained by glutamine addition throughout the culture, the methods of the current invention are also applicable except that the increased quantity of glutamine will be added gradually over the course of the culture. Recently, some researchers have found that addition of supplemental glutamine late in culture can increase culture longevity for some cell lines (S. Reuveny, et al., Factors Affecting Cell Growth and Monoclonal Antibody Production in Stirred Reactors, J. Immunol. Methods, 1986, 86:53-590). We have found that supplemental glutamine can be added either at the start of culture, or during the course of culture with the total of glutamine added to about 5-40 mmoles and preferably about 8-20 mmoles per liter. We believe that late in culture, in a post exponential growth pseudo-stationary phase, that glutamine can be a major energy source for the cells, (i.e. glutamine consumption continues while glucose consumption may decline). We find that glutamine supplementation is necessary, but not sufficient to achieve the desired increase in culture longevity. To achieve the optimal performance, glutamine must be added in combination with the other reagents of the Primary Supplement. B. Phospholipid Precursors The Primary Supplement also contains phospholipid precursors, selected from the group including but not limited to, serine, inositol, choline, ethanolamine, and glycerol. While these components are all phospholipid precursors, they also have other biochemical roles, and this invention should not be considered as being limited by any proposed hypothesis of a mechanism of action. Serine is considered an essential amino acid, and inositol an essential vitamin. Most cell culture media contain serine and inositol at adequate levels for their roles as phospholipid precursors and other biochemical roles. Choline is included as a vitamin in most media at 1-4 mg/L. However, on occasion, choline has been used at higher concentrations. For instance, to grow cells of nonlymphoid origin, Ham (R. G. Ham, Clonal Growth of Mammalian Cells in a Chemically Defined Synthetic Medium, Proc. Natl. Acad. Sci. USA, 1965, 53:288-293) includes choline at 15 mg/L in a serum-free medium for clonal growth of Chinese Hamster Ovary Cells. J.Birch, et al., J. Cell Sci., 1969, 5:135-142) includes choline at 20 mg/L in a serum containing medium for growth of mouse fibroblasts. Waymouth's (C. Waymouth, Rapid Proliferation of Sublines of NCTC Clone 929 Mouse Cells in a Simple Chemically Defined Medium, J. Natl. Cancer Inst., 1959, 22:1003-1017) medium MB 752/1 for culture of mouse L929 fibroblast connective tissue cell line is exceptional in including choline at 250 mg/L. Although Ham, Birch and Waymouth developed media to support cell growth, they did not study the production of biological products produced by cells grown in the media. We have found that cells, preferably antibody secreting cells, grow and secrete maximal amounts of antibody in media containing choline supplemented to a level of greater than about 4 mg/L, and preferably at approximately 4-75 mg/L in combination with the other reagents of the Primary Supplement. At these concentrations, choline does not become limiting and is without apparent toxicity. Ethanolamine is not typically included in serum supplemented media. Murakami (H. Murakami, et al., Proc. Natl. Acad. Sci. USA, 1982, 79:1158-1162) demonstrates that ethanolamine at 20 uM is stimulatory to growth of a murine hybridoma cell line. Tharakan, et al., J. Immunol. Methods, 1986, 94:225-235; Cole, et al., J. Immunol. Methods, 1987, 97:29-35; and Kovar, et al., Immunol. Letters, 1984, 7:339-345 also found ethanolamine to be stimulatory to growth of several murine hybridoma cell lines. None of these researchers combined elevated levels of ethanolamine with elevated levels of glutamine, choline, tryptophan and other amino acids as we have found necessary for optimum product expression. Several other serum-free media do not include ethanolamine (T. Chang, et al., J. Immunol. Methods, 1980, 39:369-375) and a review by Iscove (N. N. Iscove, Culture of Lymphocytes and Hemopoietic Cells in Serum-Free Medium p. 169-185 in Methods for Serum-Free Culture of neuronal and Lymphoid Cell Lines, Alan R. Liss Inc., NY 1984) identifies choline and inositol as essential, but does not mention ethanolamine. We have found that ethanolamine is effective when supplemented to a level of approximately 1-10 mg/L, and can be included at up to at least 20 mg/L without apparent toxicity. It should be understood that choline and ethanolamine can be provided in various forms including phosphocholine and phosphoethanolamine or phosphatidylcholine and phosphatidyletanolamine. The relative effectiveness of these various forms will depend on the ability of the specific cell line to take up (transport) and metabolize the complex forms. Supplementation of standard media with phospholipid precursors alone is not sufficient to achieve the desired maximum extension of culture longevity and product production. Rather, phospholipid precursors act in synergy with the other components described. The phospholipid precursors may be added to media as a microemulsion using a suitable emulsifier, preferably pluronic polyol F68. C. Tryptophan Tryptophan is recognized as an essential amino acid and is included in typical serum-supplemented and serum-free media at 2-20 mg/L, with the exception of Waymouth's MB752/1 medium for L-929 cells where it is present at 40 mg/L. Several researchers have attempted to optimize media by supplementation with increased levels of each amino acid added separately. Typical of these, Barns and Iscove (N. N. Iscove, Culture of Lymphocytes and Hemopoietic Cells in Serum-Free Medium p. 169-185 in Methods for Serum-Free Culture of Neuronal and Lymphoid Cells) have both tested supplementation of media with each of the standard amino acids, and neither found addition of tryptophan at greater than standard levels to be stimulatory. We have found that tryptophan supplementation is essential to achieving the desired increase in culture longevity and product titre. For optimal effect, tryptophan is supplemented to levels higher than those typically taught in the literature, or greater than 20 mg/L, and can be added at up to at least 250 mg/L without toxic effect. Supplementation of standard media with tryptophan alone is not sufficient to achieve the desired effect. Rather, tryptophan at elevated concentrations acts in synergy with the other components of the Primary Supplement to achieve the desired maximum extension of culture growth and longevity, and product production. D. Other Amino Acids The recommended Primary Supplement also includes a formulation of amino acids determined to be desirable for expression of a product from a particular cell line. Amino acids are the essential building blocks for protein synthesis. Supplementation of medium with the components specified provides the basis for increased culture longevity, and hence, for a significantly increased period for product production. Under these conditions, amino acids required for cell maintenance and product synthesis can become depleted. To maximize final product titre, the levels of these amino acids must be increased so as to not become limiting. Amino acid analysis of spent medium using techniques which are known to the analytical chemist (D. H. Speckman, et al., Automatic Recording Apparatus for Use in the Chromatography of Amino Acids, Analytical Chemistry, 1958, 30:1190-1206) can be used as a tool to identify those amino acids which are depleted during culture and require supplementation. Iscove (N. N. Iscove, Culture of Lymphocytes and hemopoietic Cells in Serum-Free Medium p. 169-185 in Methods for Serum-Free Culture of Neuronal and Lymphoid Cells) and others have tested supplementation of media with each of the standard amino acids. Typical of the literature, Iscove found that addition at greater than standard levels of all amino acids tested, (except cystine), was not stimulatory. Luan (Y. T. Luan, et al., Strategies to Extend Longevity of Hybridomas in Culture and Promote Yield of Monoclonal Antibodies) describes a fed batch strategy, consisting of adding a supplement containing glutamine, essential amino acids (including tryptophan), vitamins (including choline) and serum at various time points during the culture of a murine hybridoma cell line. The medium to which additions was made consisted of DMEM supplemented with fetal calf serum. This method resulted in an increase in culture longevity and increase in final antibody titre. Similarly, Birch (J. R. Birch, et al., Animal Cell Culture, EPA PCT/GB6/00383, 1986) describes fed-batch culture adding a supplement containing glucose, glutamine essential and non-essential amino acids (including tryptophan) during the culture of another murine hybridoma cell line. The medium to which additions was made was also DMEM supplemented with fetal calf serum. It is important to note regarding Luan and Birch that neither included ethanolamine in their media which we have found to be a highly favored phospholipid precursors for the optimum cell growth and product production effect. Further, while we have found that our supplement can be used effectively in fed-batch and continuous culture, we have found (unlike Luan and Birch) that inclusion of the supplement at the start of culture is also effective (i.e. in contrast to Luan and Birch, nutrient addition during culture is not obligatory using the supplement of the current invention). Additionally, applicants' supplement can be used advantageously with serum-free and protein-free media. Also differentiating the current work, neither Luan and Birch included a defined reducing agent, such as MTG which we have identified, as discussed below, as a preferred embodiment which can result in a further increase in cell product expression. III. Class I Reagents The reagents of the Primary Supplement can be combined with additional reagents to produce media having more favorable cell growth and product expression properties. These, or Class I reagents, include, but are not limited to, reducing agents, trace metal ions and/or vitamins. Components of the Class I reagents can be added individually or in combination with the complete set of reagents of the Primary Supplement. The utility of these additional Class I reagents will vary depending on the cell line and basal medium composition. A. Reducing Agents The metabolism of glutathione and related sulfhydryl species has been reviewed by Meister (A. Meister, Selective Modification of Glutathione Metabolism, Science, 1983, 220:472-477). Yamane (I. Yamane, et al., Effects of Sulfhydryl Groups and Oxygen Tension on the Cell Proliferating Activity of Bovine Serum Albumin in Culture, Cell Structure and Function, 1982, 7:133-143) shows that addition of reducing agents can protect cultures from damage associated with high oxygen tension. Some serum-supplemented media (such as RPMI 1640) contain added glutathione (GH) at 1-15 mg/L. Other reducing agents are not generally included in serum-supplemented media. For example, .beta.-mercaptoethanol (B-ME) and mono-thioglycerol (MTG) are not typically included in cell culture media, and are not included in any of the media tabulated by Freshey above. In contrast, glutathione or dithiothreitol (DTT) is included in MCDB 110 serum-free medium, but are absent from several other serum-free formulations (CDB 170, MCDB 153, WAJC, HITES, etc.). Iscove's serum-free medium does not contain GH or DTT. It is important to note that although there are reports of media containing reducing agents, that none of these media contain all of the reagents of the Primary Supplement. For instance, Iscove (N. N. Iscove, Culture of Lymphocytes and Hemopoietic Cells in Serum-Free Medium, p 169-185, in Methods for Serum-Free Culture of Neuronal and Lymphoid Cells) recommends supplementation of his IMDM medium with either B-ME (5.times.10.sup.-5 M) or MTG 7.5.times.10.sup.-5 M. Iscove's medium does not, however, contain ethanolamine or the elevated levels of glutamine, tryptophan and other amino acids required for the synergistic effect observed for cell growth and product expression attributed to reagents of the Primary Supplement. Further, Kawamoto (T. Kawamoto, Anal. Biochem., 1983, 130:445-453) has supplemented a basal medium with several components including ethanolamine (10 M) and B-ME (10 M). Kawamoto's media do not, however, contain the elevated levels of glutamine, tryptophan and other amino acids required for the synergistic effect. Likewise, Kovar (J. Kovar, et al., Immunol. Letters, 1984, 7:339-345) developed a serum-free medium containing ethanolamine (20 M), but this medium again contains low levels of glutamine, tryptophan and other amino acids and does not result in the synergy which we have discovered. Kovar (J. Kovar, et al., Serum-Free Medium for Hybridoma and Parental Myeloma Cell Cultivation: A Novel Composition of Growth Supporting Substances) tested .beta.-mercaptoethanol as a possible component in their ethanolamine supplemented RPMI-1640 based serum-free medium. This medium did not contain elevated levels of glutamine, tryptophan, other amino acids, or choline, which we have found favors the optimum synergistic effect. In the absence of these components, Kovar and Frank found B-ME not to be useful and deleted it from their final formulation. We have found that supplementation of culture media with a reducing agent/sulfhydryl compound can result in an increase in culture longevity and product titre. However, such supplementation is maximally effective when in combination with the complete Primary Supplement. Reducing agent/sulfhydryl compounds for use include .beta.-mercaptoethanol, monothioglycerol (MTG), dithiothreitol, glutathione, thioglycolate, and cystine. More preferred are thiol molecules which have hydroxyl group(s) such as (.beta.-mercaptoethanol) B-ME, (monothioglycerol) MTG and (dithiothreitol) DTT. Most preferred are mono-thiol compounds of this class such as B-ME and MTG. These are effective at concentrations above 0.1 mg/L and are not toxic at up to at least 10 mg/L. A preferred concentration is 0.5-100 mg/L for either B-ME or MTG. More preferred is 10 mg/l for MTG. B. Metal Ions Metal ions are essential for animal cell culture and are included in typical media as components of salt and trace element mixtures, or as components of undefined supplements such as serum (K. Higuchi, Cultivation of Animal Cells in Chemically Defined Media--A Review p. 111-136). In media supplemented with the reagents of the Primary Supplement, high cell densities can be reached such that availability of certain metal ions, if included only at the levels incorporated in standard media designed to support lower cell densities, can become limiting. Therefore, in a preferred embodiment of the current invention, metal ions are also included in the supplement as found to be necessary for a particular cell line. At the high concentrations that can be required, solubility limits of some metal ions may limit the maximum concentration that can be added with beneficial effect. Therefore, a further preferred embodiment is to supply necessary metal ions along with a suitable chelating agent. The chelating agent must be non-toxic at the concentrations added, and must bind the required metal ions in a reversible manner such that they may be held in solution at adequate concentration, but will be delivered to the cells in an active form. Analysis of the spent medium using techniques which are well known to the analytical chemist ("Flame Photometry", Chpt. 11, in H. Willard, et al., Instrumental Methods of Analysis, Van Nostrand Co., 1965) can be used as a tool to identify those metal ions which are utilized and may require supplementation. Some metal ions which may require supplementation include, but are not limited to, calcium, magnesium, molybdenum, cobalt, copper, manganese, zinc, selenium and iron. A more extensive list is given by Hamilton and Ham (W. Hamilton, et al., Clonal Growth of Chinese Hamster Cell Lines in Protein-Free Media, In Vitro, 1977, 13(9):537-547). Various metal chelators have been used in cell culture. Natural proteins which can serve this function include transferrin and ferritin, especially to chelate iron, and albumin to chelate a variety of multivalent metal ions. Some other chelators which have been used especially to chelate iron include pyridoxyl isonicotinoyl hydrazone, choline citrate, citrate (C. III, T. Brehm, et al., Species Specificity of Iron Delivery in Hybridomas, In Vitro Cell. Develop. Biol., 1988, 24(5):38) and acetylacetonate (L. Rasmussen, et al., Utilization of Iron Complexes in an Animal Cell, J. Cellular Physiol., 1985, 122:155-158). We have found citrate at about 0.1-10 mM to be an effective chelator capable of supplying several multivalent metal ions. In addition, a variety of other organic acids such as malic acid, succinic acid, fumaric acid and alpha ketoglutaric acid are effective chelators. Citrate is the preferred chelator because of its capacity to chelate iron. Indeed, in those media that are devoid of insulin and transferrin, high levels of iron are used, typically supplied to the cells as FeCl.sub.3.6H.sub.2 O or FeSO.sub.4, with high levels of citrate. For example, in Example 8, FeCl.sub.3 is 27 mg/l and Na citrate at 294 mg/l. C. Vitamins Vitamins are essential for animal cells in culture and are generally included in cell culture media (K. Higuchi, Cultivation of Animal Cells in Chemically Defined Media--A Review p. 111-136 in Advan. Appl. Microbiol., 1973, 16:111). In media supplemented only with the Primary Supplement composition, high cell densities can be reached such that availability of certain vitamins, if included only at the levels incorporated in standard media designed to support lower cell densities, can become limiting. Therefore, in a further preferred embodiment of the current invention, vitamins may also be included in the supplement as found to be necessary for a particular cell line. Vitamins which may become limiting include, but are not limited to, p-amino-benzoic acid, biotin, folic acid, folinic acid, nicotinamide, pantothenate, pyridoxine, riboflavin, flavin adenine dinucleotide, ascorbic acid, thiamine and vitamin B-12. Having generally described the media supplements of the instant invention, several limitations associated with their use, as well as ways to circumvent the limitations warrant discussion. Firstly, although it is convenient to define classes of reagents that can be readily combined with culture media that is fed to cells without later during the culture period having to refeed the cells, it will be appreciated by those skilled in the art that similar favorable effects can be gained by adding individual reagents to the culture media during the culture period, so as to maintain their concentrations at the levels provided by the supplements. This is most apparent with regard to glutamine, which can be added in combination with the other reagents of the Primary Supplement, or omitted and individually added and maintained at the desired level. Secondly, the concentrations of reagents that are used in the various supplements will vary over the ranges stated, and are a function of both the cell culture media to which the supplements are added, as well as the particular cell type cultured. The optimal concentrations of the reagents are readily determined by those skilled in the art. Thirdly, with the exception of reagents of the Primary Supplement, all of which must be present in the supplements for maximum cell culture benefit, only one of the Class I reagents need be present for maximum advantageous results. Fourthly, it will be realized that for optimal results, the basal medium to which the supplement is added must be appropriate for the cell line of interest, with key nutrients available at adequate levels to enhance cell growth or product expression. Thus, for example, it may be necessary to increase the level of glucose (or other energy source) in the basal medium, or to add glucose (or other energy source) during the course of culture, if this essential energy source is found to be depleted and to thus limit cell growth or product expression. The following examples illustrate the invention, but are not intended to limit it in any manner. For instance, hybridomas and antibodies are illustrative of cell lines that can be successfully grown and harvested, respectively in media supplemented with the instant compositions. However, such media are not limited to growing hybridomas or harvesting antibody, but rather can be used to grow a wide variety of cells that produce a broad range of products. It will further be appreciated by those skilled in the art that various components used to formulate the media presented herein can be substituted by chemically related compounds without adversely affecting the formulations. |
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