USH1532H - Adaption of mammalian cell lines to high cell densities - Google Patents

Adaption of mammalian cell lines to high cell densities Download PDF

Info

Publication number
USH1532H
USH1532H US08/146,860 US14686093A USH1532H US H1532 H USH1532 H US H1532H US 14686093 A US14686093 A US 14686093A US H1532 H USH1532 H US H1532H
Authority
US
United States
Prior art keywords
passage
cells
approximately
nutrients
culture
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US08/146,860
Inventor
S. Robert Adamson
Denis Drapeau
Yen-Tung Luan
Douglas A. Miller
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Genetics Institute LLC
Original Assignee
Genetics Institute LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Genetics Institute LLC filed Critical Genetics Institute LLC
Priority to US08/146,860 priority Critical patent/USH1532H/en
Assigned to GENETICS INSTITUTE, INC. reassignment GENETICS INSTITUTE, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MILLER, DOUGLAS A., LUAN, YEN-TUNG, DRAPEAU, DENIS, ADAMSON, S. ROBERT
Priority to AU80154/94A priority patent/AU8015494A/en
Priority to PCT/US1994/011535 priority patent/WO1995012664A1/en
Application granted granted Critical
Publication of USH1532H publication Critical patent/USH1532H/en
Assigned to GENETICS INSTITUTE, LLC reassignment GENETICS INSTITUTE, LLC CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: GENETICS INSTITUTE, INC.
Abandoned legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N5/00Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
    • C12N5/0018Culture media for cell or tissue culture
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N2500/00Specific components of cell culture medium
    • C12N2500/30Organic components
    • C12N2500/32Amino acids
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N2510/00Genetically modified cells
    • C12N2510/02Cells for production

Definitions

  • the present invention relates to improved methods of expressing proteins through culture of mammalian cell lines.
  • the present invention relates to methods of improving the productivity of mammalian cell lines through adaption to otherwise growth-limiting conditions.
  • the previous methods have several drawbacks. First, in order to generate tolerance to an inhibitor according to the above methods, it is first necessary to determine that a particular inhibitor is a growth-limiting factor for cells and then to develop a protocol for generating tolerance to that inhibitor. Second, the growth of cell lines which are generated with tolerance to a particular inhibitor according to the above methods may then be limited by a second, different inhibitor. Repeated experiments may be necessary to generate tolerance to multiple growth-limiting inhibitors in order to achieve significant increases in cell densities.
  • the present invention provides methods by which the growth-limiting factors present for a particular cell line can be overcome without first conducting time-consuming testing to identify the specific growth-limiting inhibitors.
  • the above objects are largely achieved by providing methods for adapting mammalian cell lines to culture at increased cell densities.
  • the methods of the present invention comprise adapting mammalian cell lines to grow at increased cell densities, by (a) initiating a passage by diluting a culture containing mammalian cells with a suitable growth medium by a dilution factor suitable for the passage duration; (b) maintaining pH, dissolved oxygen, and nutrients at non-limiting levels during the passage; and repeating steps (a) and (b) at least about 5 times. In a preferred embodiment of the invention, the steps are repeated about 5 to about 20 times.
  • the present invention further comprises methods for adapting CHO cell lines to grow to increased cell densities, comprising:
  • the present invention further comprises methods for adapting CHO cell lines to grow to increased cell densities comprising: (a) initiating a passage of duration approximately 3 to 4 days by diluting a culture containing CHO cells at a density of at least approximately 1 ⁇ 10 6 cells/ml with a suitable growth medium, the dilution factor being suitable to the passage duration; (b) maintaining pH, dissolved oxygen, and nutrients at non-limiting levels during the passage; and (c) repeating steps (a) and (b) at least about 5 times.
  • the present invention comprises a method for adapting mammalian cell lines to culture at increased cell densities, said method comprising continuously or periodically diluting a cell culture, containing mammalian cells, with a suitable growth medium, for between approximately 10 and 60 days, while maintaining pH, dissolved oxygen and nutrients at non-limiting levels.
  • kits for the present invention comprise adapting CHO cell lines to culture at increased cell densities, said method comprising continuously or periodically diluting a culture containing CHO cells, at a density of at least approximately 1 ⁇ 10 6 cells/ml with a suitable growth medium, the dilution rate being less than approximately 0.029 hr -1 , while maintaining pH, dissolved oxygen and nutrients at non-limiting levels.
  • Preferred dilution rates are between approximately 0.018hr -1 and 0.026hr -1 .
  • Mammalian cell lines are used for the production of commercially useful proteins. Some mammalian cell lines which are commonly used include chinese hamster ovary (CHO) cell lines, hybridomas, monkey COS-1 cells, HeLa cells, melanoma cell lines such as the Bowes cell line, hybridoma cell lines, mouse L cells, mouse fibroblasts, mouse NIH 3T3 cells and the CV-1 cell line. In the present invention, these and other mammalian cell lines may be adapted for culture at high cell densities.
  • CHO chinese hamster ovary
  • Suitable growth media for the present invention include any medium which provides nutrients at non-limiting levels. Nutrients will generally be at non-limiting levels if raising concentrations of all nutrients results in no increase in growth rate. Nutrient concentrations may be maintained at non-limiting levels by either providing excess amounts of all nutrients in the fresh medium or by adding nutrients to the culture as they are taken up by the cells or degraded.
  • a suitable growth medium for mammalian cell lines is disclosed in Ling et al., Experimental Cell Research; 52:469-489 (1968). Accordingly, one preferred growth medium contains the amino acid nutrients in the concentrations disclosed in Table 1.
  • nutrients which may be addded to the medium include inorganic salts, such as chlorides, phosphates, sulfates and nitrates, sugars, vitamins, and additives such as glutamine, pyruvate, linoleic, thioctic, selenite, hydrocortisone, insulin.
  • inorganic salts such as chlorides, phosphates, sulfates and nitrates
  • sugars such as glutamine, pyruvate, linoleic, thioctic, selenite, hydrocortisone, insulin.
  • growth media suitable for mammalian cell lines include a medium containing the components described in Table 2 below.
  • Suitable dilution factors (for passaging) and suitable dilution rates (for continuous culture) appropriate for adapting a particular mammalian cell line to grow to increased cell densities may be calculated using the formulas:
  • ⁇ max in hour -1 is the specific growth rate of the cell line when none of the following extracellular factors limits growth: pH, dissolved oxygen, nutrient depletion and cell-generated inhibitors.
  • the magnitude of ⁇ max may be estimated without precise measurement in a variety of ways.
  • an estimate of ⁇ max may be generated as follows. First the maximum cell density attainable in a spinner flask using a common medium (such as a 1:1 mixture of DME and F12) is determined by suspending growth phase cells in this medium in the spinner flask and measuring the cell density on each subsequent day until cell density no longer rises. Next, growth phase cells are suspended in fresh medium in another spinner flask at a starting density approximately 10-fold below the maximum attainable density and cultured for approximately 2 days. This culture is diluted with fresh medium to the same starting cell density every two days for several passages. The estimate of ⁇ max is the growth rate observed during these passages, calculated using the following formula:
  • X r is the cell density at the end of a typical passage
  • X i is the cell density at the beginning of the same passage
  • t is the duration of the passage in hours.
  • a suitable dilution factor for a given duration of passage may be as follows: If the passage is approximately 1 day, a suitable dilution factor is less than about 2, preferably from about 1.5 to about 2. If the passage duration is approximately 2 days, a suitable dilution factor is less than about 4, preferably from about 2 to about 4. If the passage duration is approximately 3 days, a suitable dilution factor is less than about 8, preferably from about 3 to about 7. If the passage duration is approximately 4 days, suitable dilution factors are less than about 16, preferably from about 5 to about 13. If the passage duration is approximately 5 days, a suitable dilution factor is less than about 32, preferably from about 9 to about 23. For other mammalian cell lines, suitable dilution factors may be calculated on the basis of the maximum growth rate of the cell line. The maximum growth rate for a cell line may be determined as described above.
  • relatively constant levels of pH, dissolved oxygen, and nutrients are maintained at non-limiting levels during the passage. This may preferably be accomplished by performing the adaption process in a bioreactor. pH may be maintained at the proper pH by addition of a suitable alkaline or acidic additive or buffer, for example sodium carbonate and sodium bicarbonate. Dissolved oxygen may be maintained by introduction of oxygen or air bubbles. If necessary, nutrient levels may be maintained by the addition of those nutrients which are depleted, or by addition of fresh growth medium.
  • mammalian cell lines such as CHO cell lines
  • a suitable cell density which may be approximately 1 ⁇ 10 6 cells/ml, in a suitable growth medium, and may be diluted in accordance with the above description.
  • the recombinant chinese hamster ovary cell (CHO) line E5F3G expresses recombinant human M-CSF, as described in Clark et at., U.S. Pat. Nos. 4,868,119 and 4,879,227. As described below, the E5F3G cell line was adapted to grow to increased cell densities, and thereby generate higher concentrations of rhM-CSF.
  • E5F3G cells from a spinner flask were grown to a density of 1.24 ⁇ 10 6 cells/ml in approximately 1000 ml of a nutrient-rich medium (Table 2) in a 2-L bioreactor (passage 1 in Table 3).
  • passage 12 which was started at a density of 0.50 ⁇ 10 6 cells/ml
  • cell density reached 4.90 ⁇ 10 6 cells/ml
  • rhM-CSF titer reached 32.6 ug/ml.
  • passage 4 which had been started at a higher cell density (0.59 ⁇ 10 6 cells/ml)
  • cell density had reached only 2.44 ⁇ 10 6 cells/ml
  • rhM-CSF titer had reached only 14.9 ug/ml.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Biotechnology (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Genetics & Genomics (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Cell Biology (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

Methods and nutrient media are disclosed useful for adapting mammalian cell lines to culture at increased cell densities.

Description

FIELD OF THE INVENTION
The present invention relates to improved methods of expressing proteins through culture of mammalian cell lines. In particular, the present invention relates to methods of improving the productivity of mammalian cell lines through adaption to otherwise growth-limiting conditions.
BACKGROUND OF THE INVENTION
It is known that various factors may be responsible for limiting the growth of cells at high cell densities. These factors include absence of sufficient amounts of nutrients needed by the cells for sustained growth, as well as the presence of growth-limiting concentrations of inhibitors that may be secreted by the cells in culture. One inhibitor that is secreted by mammalian cells is ammonia. See Miller et at., Bioprocess Engineering, 3:113-122 (1988); Inlow et at., U.S. Pat. No. 5,156,964 describes a method for generating tolerance to ammonia that involves culturing cells in a medium to which ammonia has been added. Similarly, Schumpp et at., Cytotechnology, 8:39-44 (1992) describe a method for generating cell lines tolerant of both ammonia and lactic acid by culturing cells in a medium to which both ammonia and lactic acid had been added.
The previous methods have several drawbacks. First, in order to generate tolerance to an inhibitor according to the above methods, it is first necessary to determine that a particular inhibitor is a growth-limiting factor for cells and then to develop a protocol for generating tolerance to that inhibitor. Second, the growth of cell lines which are generated with tolerance to a particular inhibitor according to the above methods may then be limited by a second, different inhibitor. Repeated experiments may be necessary to generate tolerance to multiple growth-limiting inhibitors in order to achieve significant increases in cell densities.
SUMMARY OF THE INVENTION
According to the present invention, many of the drawbacks of the above prior art are overcome. The present invention provides methods by which the growth-limiting factors present for a particular cell line can be overcome without first conducting time-consuming testing to identify the specific growth-limiting inhibitors.
It is one object of the present invention to provide methods of improving the productivity of mammalian cell lines.
It is another object of the present invention to provide methods for adapting cell lines to high cell densities.
It is yet another object of the present invention to provide nutrient-rich growth media in which nutrients are present in sufficient quantity so that they are not expected to limit cell growth.
According to the present invention, the above objects are largely achieved by providing methods for adapting mammalian cell lines to culture at increased cell densities. The methods of the present invention comprise adapting mammalian cell lines to grow at increased cell densities, by (a) initiating a passage by diluting a culture containing mammalian cells with a suitable growth medium by a dilution factor suitable for the passage duration; (b) maintaining pH, dissolved oxygen, and nutrients at non-limiting levels during the passage; and repeating steps (a) and (b) at least about 5 times. In a preferred embodiment of the invention, the steps are repeated about 5 to about 20 times.
The present invention further comprises methods for adapting CHO cell lines to grow to increased cell densities, comprising:
a) initiating a passage of duration aproximately 1 to 5 days by diluting a culture containing CHO cells at a density of at least approximately 1×106 cells/ml with a suitable growth medium, the dilution factor being suitable to the passage duration; (b) maintaining pH, dissolved oxygen, and nutrients in non-limiting levels during the passage; and
c) repeating steps (a) and (b) at least about 5 times.
The present invention further comprises methods for adapting CHO cell lines to grow to increased cell densities comprising: (a) initiating a passage of duration approximately 3 to 4 days by diluting a culture containing CHO cells at a density of at least approximately 1×106 cells/ml with a suitable growth medium, the dilution factor being suitable to the passage duration; (b) maintaining pH, dissolved oxygen, and nutrients at non-limiting levels during the passage; and (c) repeating steps (a) and (b) at least about 5 times.
In a preferred embodiment, the present invention comprises a method for adapting mammalian cell lines to culture at increased cell densities, said method comprising continuously or periodically diluting a cell culture, containing mammalian cells, with a suitable growth medium, for between approximately 10 and 60 days, while maintaining pH, dissolved oxygen and nutrients at non-limiting levels.
Other preferred methods of the present invention comprise adapting CHO cell lines to culture at increased cell densities, said method comprising continuously or periodically diluting a culture containing CHO cells, at a density of at least approximately 1×106 cells/ml with a suitable growth medium, the dilution rate being less than approximately 0.029 hr-1, while maintaining pH, dissolved oxygen and nutrients at non-limiting levels. Preferred dilution rates are between approximately 0.018hr-1 and 0.026hr-1.
DETAILED DESCRIPTION OF THE INVENTION
Mammalian cell lines are used for the production of commercially useful proteins. Some mammalian cell lines which are commonly used include chinese hamster ovary (CHO) cell lines, hybridomas, monkey COS-1 cells, HeLa cells, melanoma cell lines such as the Bowes cell line, hybridoma cell lines, mouse L cells, mouse fibroblasts, mouse NIH 3T3 cells and the CV-1 cell line. In the present invention, these and other mammalian cell lines may be adapted for culture at high cell densities.
Suitable growth media for the present invention include any medium which provides nutrients at non-limiting levels. Nutrients will generally be at non-limiting levels if raising concentrations of all nutrients results in no increase in growth rate. Nutrient concentrations may be maintained at non-limiting levels by either providing excess amounts of all nutrients in the fresh medium or by adding nutrients to the culture as they are taken up by the cells or degraded. A suitable growth medium for mammalian cell lines is disclosed in Ling et al., Experimental Cell Research; 52:469-489 (1968). Accordingly, one preferred growth medium contains the amino acid nutrients in the concentrations disclosed in Table 1.
              TABLE 1
______________________________________
              Column II
              CONCEN-   Column III
              TRATION   OPTIMAL
Column I      RANGE     CONCENTRATION
NUTRIENT      (MG/L)    (MG/L)
______________________________________
L-asparagine H.sub.2 O
              30-360    540
L-aspartic acid
              69-798    266
Glycine       30-450     60
L-isoleucine  79-948    472
L-leucine     158-1890  681
L-lysine HCl  229-2742  728
L-methionine  75-894    238
L-serine      79-948    630
L-threoine     90-1074  381
L-tryptophan  31-366    131
L-tyrosine 2Na 2H.sub.2 O
              65-783    418
L-valine      141-1686  374
______________________________________
Other nutrients which may be addded to the medium include inorganic salts, such as chlorides, phosphates, sulfates and nitrates, sugars, vitamins, and additives such as glutamine, pyruvate, linoleic, thioctic, selenite, hydrocortisone, insulin.
Other preferred growth media suitable for mammalian cell lines include a medium containing the components described in Table 2 below.
                                  TABLE 2
__________________________________________________________________________
NUTRIENT COMPOSITION OF MEDIUM
                  Column II
                  Medium Column II
                                Column IV
                  proposed by
                         Medium used
                                Preferred
                  Ling et al.
                         for adaptation
                                non-limiting
Column I          (mg/L) in Example
                                medium
Components        (1968) (mg/L) (mg/L)
__________________________________________________________________________
sodium chloride   7000   4600   4400
potassium chloride
                  375    624    310
calcium chloride, anhydrous
                  156    232    58
sodium phosphate, dibasic, anhydrous
                         142
sodium phosphate, monobasic, hydrate
                         125    130
magnesium chloride, anhydrous
                         57
magnesium sulfate, anhydrous
                  120    98     84
cupric sulfate, anhydrous
                  185    0.0016 0.0018
ferrous sulfate, anhydrous
                         0.68   0.91
ferric nitrate, nonahydrate
                  1.2    0.10
zinc sulfate, septahydrate
                  0.86   0.86   0.92
sodium selenite          0.010  0.010
sodium bicarbonate       2440   2400
L-alanine         45-534 36     71
L-arginine        218-2616
                         600    760
L-asparagine hydrate
                  30-360 180    540
L-aspartic acid   67-798 133    270
L-cysteine hydrochloride hydrate
                         282    700
L-cystine dihydrochloride
                  23-281 125
L-glutamic acid   103-1236
                         59     120
L-glutamine       212-2544
                         1168   1200
glycine           38-450 60     60
L-histidine hydrochloride hydrate
                  105-1260
                         126    290
L-isoleucine      79-948 210    470
L-leucine         158-1890
                         260    680
L-lysine hydrochloride
                  229-2742
                         291    730
L-methionine      75-894 104    240
L-phyenylalanine   99-1188
                         165    330
L-proline          86-1032
                         138    280
L-serine          79-948 315    630
L-threoinie        90-1074
                         190    380
L-tryptophan      31-366 33     130
L-tryosine disodium dihydrate
                  57-678 262    420
L-valine          141-1686
                         187    370
biotin            0.03   0.41   1.6
D-calcium pantothenate
                  5.0    4.5    18
choline chloride  350    18     72
folic acid        0.10   5.3    21
i-inositol        35     25     100
nicotinamide      20     4.0    16
pyridoxine hydrochloride 0.062  16
pyridoxal hydrochloride
                  2.5    4.0
riboflavin        1.5    0.44   1.8
thiamine hydrochloride
                  1.0    4.3    18
vitamin B12       0.003  1.6    5.6
D-glucose         2000   6000   6200
sodium pyruvate          110
linoleic acid     0.21   0.084  0.17
thioctic acid     0.70   0.21   0.42
putrescine dihydrochloride
                         2.2    2.0
polyvinyl alcohol        2400   2400
insulin or Nucellin
                  1.0    10     10
hydrocortisone           0.072  0.072
methotrexate             1.3
soybean phospholipid     10
fetal bovine serum       5000
B-glycerophosphate, disodium
                  1000
D-sorbitol        100
oxalacetic acid   65
thymidine         10
deoxycytidine     11
homocysteine thiolactate
                  8-90
glutathione, reduced
                  31-372
sodium molybdate, dihydrate
                  0.015
vitamin A acetate 1.0
vitamin D3        0.005
a-tocopherol      7.0
oleic acid        0.2
arachidonate, methyl
                  0.02
cholesterol       5
ovo-lecithin      25
ethanol           2000
__________________________________________________________________________
Suitable dilution factors (for passaging) and suitable dilution rates (for continuous culture) appropriate for adapting a particular mammalian cell line to grow to increased cell densities may be calculated using the formulas:
dilution factor=e.sup.(μt)
dilution rate=μ
where t is the duration in hours of the upcoming passage and μ is any quantity less than μmax, preferably a quantity between approximately (0.6×μmax) and approximately (0.9×μmax). μmax in hour-1, is the specific growth rate of the cell line when none of the following extracellular factors limits growth: pH, dissolved oxygen, nutrient depletion and cell-generated inhibitors.
The magnitude of μmax may be estimated without precise measurement in a variety of ways. For example, an estimate ofμmax may be generated as follows. First the maximum cell density attainable in a spinner flask using a common medium (such as a 1:1 mixture of DME and F12) is determined by suspending growth phase cells in this medium in the spinner flask and measuring the cell density on each subsequent day until cell density no longer rises. Next, growth phase cells are suspended in fresh medium in another spinner flask at a starting density approximately 10-fold below the maximum attainable density and cultured for approximately 2 days. This culture is diluted with fresh medium to the same starting cell density every two days for several passages. The estimate of μmax is the growth rate observed during these passages, calculated using the following formula:
μmax=(ln X.sub.f -ln X.sub.i)/t
where Xr is the cell density at the end of a typical passage, Xi is the cell density at the beginning of the same passage, and t is the duration of the passage in hours.
For CHO cell lines, a suitable dilution factor for a given duration of passage may be as follows: If the passage is approximately 1 day, a suitable dilution factor is less than about 2, preferably from about 1.5 to about 2. If the passage duration is approximately 2 days, a suitable dilution factor is less than about 4, preferably from about 2 to about 4. If the passage duration is approximately 3 days, a suitable dilution factor is less than about 8, preferably from about 3 to about 7. If the passage duration is approximately 4 days, suitable dilution factors are less than about 16, preferably from about 5 to about 13. If the passage duration is approximately 5 days, a suitable dilution factor is less than about 32, preferably from about 9 to about 23. For other mammalian cell lines, suitable dilution factors may be calculated on the basis of the maximum growth rate of the cell line. The maximum growth rate for a cell line may be determined as described above.
In the method of the present invention, relatively constant levels of pH, dissolved oxygen, and nutrients are maintained at non-limiting levels during the passage. This may preferably be accomplished by performing the adaption process in a bioreactor. pH may be maintained at the proper pH by addition of a suitable alkaline or acidic additive or buffer, for example sodium carbonate and sodium bicarbonate. Dissolved oxygen may be maintained by introduction of oxygen or air bubbles. If necessary, nutrient levels may be maintained by the addition of those nutrients which are depleted, or by addition of fresh growth medium.
In the present invention, mammalian cell lines, such as CHO cell lines, may be cultured at a suitable cell density, which may be approximately 1×106 cells/ml, in a suitable growth medium, and may be diluted in accordance with the above description.
The present invention is illustrated by the following examples. These examples do not limit the invention in any manner. It is contemplated that minor improvements and variations may be made which are part of the present invention.
EXAMPLES
The recombinant chinese hamster ovary cell (CHO) line E5F3G expresses recombinant human M-CSF, as described in Clark et at., U.S. Pat. Nos. 4,868,119 and 4,879,227. As described below, the E5F3G cell line was adapted to grow to increased cell densities, and thereby generate higher concentrations of rhM-CSF.
E5F3G cells from a spinner flask were grown to a density of 1.24×106 cells/ml in approximately 1000 ml of a nutrient-rich medium (Table 2) in a 2-L bioreactor (passage 1 in Table 3).
These cells were then cultured for an additional ten 3-day or 4-day passages in the 2-L bioreactor (passages 2 through 11) in the nutrient-rich medium. During each passage, pH was maintained at between 7.0 and 7.2 by addition of sodium carbonate and sodium bicarbonate and dissolved oxygen was maintained at between 20% and 60% of air saturation by introduction of oxygen bubbles. Each 3-day passage was started by diluting the culture from the preceding passage by a factor between 5.1 and 6.3, while each 4-day passage was started by diluting the culture from the preceding passage by a factor between 6.0 and 14.3.
The beneficial effect on the cell line was evident during two subsequent passages (passages 12 and 13). For example, in passage 12, which was started at a density of 0.50×106 cells/ml, cell density reached 4.90×106 cells/ml, and rhM-CSF titer reached 32.6 ug/ml. In contrast, in passage 4, which had been started at a higher cell density (0.59×106 cells/ml), cell density had reached only 2.44×106 cells/ml and rhM-CSF titer had reached only 14.9 ug/ml.
              TABLE 3
______________________________________
Adaptation of E5F3G cell line to increased cell densities
       Passage           Initial
                                Final
Passage
       length   Dilution density
                                density
                                       Final titer
number (days)   ratio    (10.sup.6 /ml)
                                (10.sup.6 /ml)
                                       (ug/ml)
______________________________________
1      4        --       0.12   1.24   11.6
2      3        5.4      0.23   1.96   14.3
3      3        6.3      0.31   3.00   16.5
4      3        5.1      0.59   2.44   14.9
5      4        12.2     0.20   1.79   --
6      4        6.0      0.30   3.50   --
7      3        5.0      0.70   2.25   12.2
8      3        5.2      0.43   2.70   15.6
9      4        12.3     0.22   4.30   20.2
10     4        14.3     0.30   5.90   29.2
11     3        5.9      1.00   5.70   33.5
12     3        11.4     0.50   4.90   32.6
13     4        16.3     0.30   5.30   34.2
______________________________________

Claims (9)

We claim:
1. A method for producing an adapted mammalian cell line which grows at increased cell densities, said method comprising:
a) initiating a passage by diluting a culture containing mammalian cells with a suitable growth medium, the dilution factor being suitable for the duration of the passage;
b) maintaining pH, dissolved oxygen, and nutrients at non-limiting levels during the passage;
c) repeating steps (a) and (b) at least about 5 times; and
d) obtaining an adapted mammalian cell line with the ability to grow at increased cell densities.
2. The method of claim 1, wherein steps (a) and (b) are repeated about 5 to about 20 times.
3. A method for producing an adapted CHO cell line which grows at increased cell densities, said method comprising:
a) initiating a passage approximately 1 to 5 days in duration by diluting a culture containing CHO cells at a density of at least approximately 1×106 cells/ml with a suitable growth medium, the dilution factor being suitable for the duration of the passage;
b) maintaining pH, dissolved oxygen, and nutrients in non-limiting levels during the passage;
c) repeating steps (a) and (b) at least about 5 times; and
d) obtaining an adapted CHO cell line with the ability to grow at increased cell densities.
4. The method of claim 3, wherein steps (a) and (b) are repeated about 5 to about 20 times.
5. A method for producing an adapted CHO cell line which grows at increased cell densities, said method comprising:
a) initiating a passage approximately 3 to 4 days in duration by diluting a culture containing CHO cells at a density of at least approximately 1×106 cells/ml with a suitable growth medium, the dilution factor being suitable to the duration of the passage;
b) maintaining pH, dissolved oxygen, and nutrients at non-limiting levels during the passage;
c) repeating steps (a) and (b) at least about 5 times; and
d) obtaining an adapted CHO cell line with the ability to grow at increased cell densities.
6. The method of claim 5, wherein steps (a) and (b) are repeated about 5 to about 20 times.
7. A method for adapting mammalian cell lines to culture at increased cell densities, said method comprising continuously or periodically diluting a cell culture, containing mammalian cells, with a suitable growth medium, for between approximately 10 to 60 days, while maintaining pH, dissolved oxygen and nutrients at non-limiting levels.
8. A method for adapting CHO cell lines to culture at increased cell densities, said method comprising continuously or periodically diluting a culture containing CHO cells, at a density of at least approximately 1×106 cells/ml with a suitable growth medium, at a dilution rate less than approximately 0.029 hr-1, while maintaining pH, dissolved oxygen and nutrients at non-limiting levels.
9. The method of claim 8, wherein the dilution rate is between approximately 0.018 hr-1 and 0.026 hr-1.
US08/146,860 1993-11-03 1993-11-03 Adaption of mammalian cell lines to high cell densities Abandoned USH1532H (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US08/146,860 USH1532H (en) 1993-11-03 1993-11-03 Adaption of mammalian cell lines to high cell densities
AU80154/94A AU8015494A (en) 1993-11-03 1994-10-12 Adaption of mammalian cell lines to high cell densities
PCT/US1994/011535 WO1995012664A1 (en) 1993-11-03 1994-10-12 Adaption of mammalian cell lines to high cell densities

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/146,860 USH1532H (en) 1993-11-03 1993-11-03 Adaption of mammalian cell lines to high cell densities

Publications (1)

Publication Number Publication Date
USH1532H true USH1532H (en) 1996-05-07

Family

ID=22519293

Family Applications (1)

Application Number Title Priority Date Filing Date
US08/146,860 Abandoned USH1532H (en) 1993-11-03 1993-11-03 Adaption of mammalian cell lines to high cell densities

Country Status (3)

Country Link
US (1) USH1532H (en)
AU (1) AU8015494A (en)
WO (1) WO1995012664A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110343666A (en) * 2019-07-10 2019-10-18 通化东宝生物科技有限公司 A kind of supplemented medium and its preparation method and application of Chinese hamster ovary celI culture

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6150328A (en) 1986-07-01 2000-11-21 Genetics Institute, Inc. BMP products
US6291206B1 (en) 1993-09-17 2001-09-18 Genetics Institute, Inc. BMP receptor proteins
WO1995016035A2 (en) 1993-12-07 1995-06-15 Genetics Institute, Inc. Bmp-12, bmp-13 and tendon-inducing compositions thereof
US6727224B1 (en) 1999-02-01 2004-04-27 Genetics Institute, Llc. Methods and compositions for healing and repair of articular cartilage
EP2286847A1 (en) 1999-10-15 2011-02-23 Genetics Institute, LLC Formulations of hyaluronic acid for delivery of osteogenic proteins
ES2305246T3 (en) 2001-06-01 2008-11-01 Wyeth COMPOSITIONS FOR THE SYSTEMIC ADMINISTRATION OF SEQUENCES CODING OSEAS MORPHOGENETIC PROTEINS.
TWI267378B (en) 2001-06-08 2006-12-01 Wyeth Corp Calcium phosphate delivery vehicles for osteoinductive proteins
BRPI0518449A2 (en) * 2004-11-19 2008-11-18 Biogen Idec Inc Methods to Produce Mammalian Cells
TWI369401B (en) * 2005-07-05 2012-08-01 Ares Trading Sa Serum-free culture medium for the production of recombinant gonadotropins
EP2078071B1 (en) 2006-11-08 2015-03-18 Wyeth LLC Rationally designed media for cell culture
MX2012004682A (en) 2009-10-26 2012-09-07 Hoffmann La Roche Method for the production of a glycosylated immunoglobulin.
WO2011134921A1 (en) 2010-04-26 2011-11-03 Novartis Ag Improved cell culture medium
KR101828624B1 (en) 2010-04-26 2018-02-12 노파르티스 아게 Improved cell cultivation process

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2195655A (en) * 1985-06-28 1988-04-13 Celltech Ltd Animal cell culture
US4757005A (en) * 1984-04-19 1988-07-12 Miles Inc. Method and cell line for obtaining plasminogen activators
US4767704A (en) * 1983-10-07 1988-08-30 Columbia University In The City Of New York Protein-free culture medium
WO1991011508A1 (en) * 1990-02-01 1991-08-08 Akzo N.V. Method for culturing cells
US5096816A (en) * 1990-06-05 1992-03-17 Cetus Corporation In vitro management of ammonia's effect on glycosylation of cell products through pH control
EP0481791A2 (en) * 1990-10-17 1992-04-22 The Wellcome Foundation Limited Culture medium for CHO-cells and adapted CHO-cells
US5122469A (en) * 1990-10-03 1992-06-16 Genentech, Inc. Method for culturing Chinese hamster ovary cells to improve production of recombinant proteins
WO1992013067A1 (en) * 1991-01-21 1992-08-06 Genzyme Corporation Production of enzymatically active glucocerebrosidase from recombinant cells
US5147790A (en) * 1982-12-30 1992-09-15 T-Pa Technology Trust Serum-independent human cell lines, process for producing same, and processes for producing proteins therefrom
US5156964A (en) * 1990-08-16 1992-10-20 Cetus Corporation Methods for adapting cells for increased product production through exposure to ammonia
WO1993005145A1 (en) * 1991-08-30 1993-03-18 Celltech Limited Cell culture process and medium for the growth of adherent animal cells

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850748A (en) * 1973-06-28 1974-11-26 Lilly Co Eli Method of producing animal cells in suspension culture
GB2251249B (en) * 1990-12-28 1995-06-21 Mogam Biotech Res Inst High-density medium for animal cell culture

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5147790A (en) * 1982-12-30 1992-09-15 T-Pa Technology Trust Serum-independent human cell lines, process for producing same, and processes for producing proteins therefrom
US4767704A (en) * 1983-10-07 1988-08-30 Columbia University In The City Of New York Protein-free culture medium
US4757005A (en) * 1984-04-19 1988-07-12 Miles Inc. Method and cell line for obtaining plasminogen activators
GB2195655A (en) * 1985-06-28 1988-04-13 Celltech Ltd Animal cell culture
WO1991011508A1 (en) * 1990-02-01 1991-08-08 Akzo N.V. Method for culturing cells
US5096816A (en) * 1990-06-05 1992-03-17 Cetus Corporation In vitro management of ammonia's effect on glycosylation of cell products through pH control
US5156964A (en) * 1990-08-16 1992-10-20 Cetus Corporation Methods for adapting cells for increased product production through exposure to ammonia
US5122469A (en) * 1990-10-03 1992-06-16 Genentech, Inc. Method for culturing Chinese hamster ovary cells to improve production of recombinant proteins
EP0481791A2 (en) * 1990-10-17 1992-04-22 The Wellcome Foundation Limited Culture medium for CHO-cells and adapted CHO-cells
WO1992013067A1 (en) * 1991-01-21 1992-08-06 Genzyme Corporation Production of enzymatically active glucocerebrosidase from recombinant cells
WO1993005145A1 (en) * 1991-08-30 1993-03-18 Celltech Limited Cell culture process and medium for the growth of adherent animal cells

Non-Patent Citations (16)

* Cited by examiner, † Cited by third party
Title
Avgerinos et al, BioTechnology, vol. 8, Jan. 1990, pp. 54 58. *
Avgerinos et al, BioTechnology, vol. 8, Jan. 1990, pp. 54-58.
Dawson, Cell Culture, edited by Butler et al, Chapter 2, pp. 25 27 and 222 (1992). *
Dawson, Cell Culture, edited by Butler et al, Chapter 2, pp. 25-27 and 222 (1992).
Griffiths, Animal Cell Culture, edited by Freshney, Chapter 3, pp. 33 45 (1986). *
Griffiths, Animal Cell Culture, edited by Freshney, Chapter 3, pp. 33-45 (1986).
Hamilton et al., In Vitro v. 13, No. 9 pp. 537 547 (1977). *
Hamilton et al., In Vitro v. 13, No. 9 pp. 537-547 (1977).
Ling et al., Experimental Cell Research v. 52 pp. 469 489 (1968). *
Ling et al., Experimental Cell Research v. 52 pp. 469-489 (1968).
Miller et al, American Chemical Society Abstracts of Papers, Part 1. Mar. 28 Apr. 2, 1993 (abstract 104). *
Miller et al, American Chemical Society Abstracts of Papers, Part 1. Mar. 28-Apr. 2, 1993 (abstract 104).
Miller et al., Bioprocess Engineering v. 3 pp. 113 122 (1988). *
Miller et al., Bioprocess Engineering v. 3 pp. 113-122 (1988).
Schumpp et al., Cytotechnology v. 8 pp. 39 44 (1992). *
Schumpp et al., Cytotechnology v. 8 pp. 39-44 (1992).

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110343666A (en) * 2019-07-10 2019-10-18 通化东宝生物科技有限公司 A kind of supplemented medium and its preparation method and application of Chinese hamster ovary celI culture
CN110343666B (en) * 2019-07-10 2023-05-30 通化东宝药业股份有限公司 Feed supplement culture medium for CHO cell culture and preparation method and application thereof

Also Published As

Publication number Publication date
WO1995012664A1 (en) 1995-05-11
AU8015494A (en) 1995-05-23

Similar Documents

Publication Publication Date Title
USH1532H (en) Adaption of mammalian cell lines to high cell densities
US6406909B1 (en) Serum-free medium for culturing animal cells
KR101264940B1 (en) Medium and culture of embryonic stem cells
Reuveny et al. Factors affecting cell growth and monoclonal antibody production in stirred reactors
CN109337861B (en) CHO cell serum-free medium supporting high expression of product
Ljunggren et al. Catabolic control of hybridoma cells by glucose and glutamine limited fed batch cultures
CA2578137A1 (en) Production of .alpha.-abeta
JP5431361B2 (en) Improved culture medium additive and method of using the same
EP0501435B1 (en) A serum-free medium for culturing animal cells
JP6393267B2 (en) Methods and systems for optimizing perfused cell culture systems
Zhang et al. A novel function for selenium in biological system: selenite as a highly effective iron carrier for Chinese hamster ovary cell growth and monoclonal antibody production
RU2007108717A (en) OBTAINING RECOMBINANT PROTEIN RFNO-LG
SG185038A1 (en) Improved cell culture medium
JPS63267269A (en) Basal nutrition medium for cell culture
CN101182490A (en) Culture medium used for Vero cell and cultivation method thereof
CN101195817A (en) Hybrid tumor cell amplification culture medium and uses thereof
US12312605B2 (en) Riboflavin derivative-containing medium
Spens et al. Defined protein and animal component‐free NS0 fed‐batch culture
EP0659880B1 (en) Medium for culturing animal cells or antibody-producing cells
JPH0728728B2 (en) Cell growth medium supplement for growing cells in vitro and method therefor
CN110117573A (en) A kind of serum-free cell culture medium and its application
EP0511226B1 (en) Process for high cell density fermentation of escherichia coli in an agitated boiler fermenter
US5916809A (en) Medium for culturing normal human epidermal melanocytes
CN107119017B (en) Serum-free culture medium for osteosarcoma cells and preparation method thereof
JPH03266981A (en) Synthetic medium for animal cell

Legal Events

Date Code Title Description
AS Assignment

Owner name: GENETICS INSTITUTE, INC., MASSACHUSETTS

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:ADAMSON, S. ROBERT;DRAPEAU, DENIS;LUAN, YEN-TUNG;AND OTHERS;REEL/FRAME:006774/0331;SIGNING DATES FROM 19931025 TO 19931102

STCF Information on status: patent grant

Free format text: PATENTED CASE

AS Assignment

Owner name: GENETICS INSTITUTE, LLC, MASSACHUSETTS

Free format text: CHANGE OF NAME;ASSIGNOR:GENETICS INSTITUTE, INC.;REEL/FRAME:012772/0631

Effective date: 20020101