IP Library Patent Application 13120558
Patent Application
App. No. 13/120,558

HIGH TITER ANTIBODY PRODUCTION

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Patent No.
US None
App. No.
13/120,558
Abstract

The present invention provides, in part, methods for recombinantly expressing proteins at a high level along with cell culture media for doing the same.

Claims (983)

1 . A method for producing a protein comprising inoculating an initial mammalian cell growth medium with host cells expressing the protein and adding supplements comprising:

Glucose;

L-glutamine;

Soy hydrolysate or wheat hydrolysate or both;

Adenine sulfate;

Adenosine;

ammonium vanadate;

Biotin;

Choline Chloride;

Cobalt chloride;

Cupric sulfate;

Cytidine;

D-Calcium Pantothenate;

Ethanolamine HCl;

Flavin Adenine Dinucleotide;

Folic Acid;

Glycine;

Guanosine;

Hypoxanthine;

i-Inositol;

L-alanine;

L-arginine;

L-asparagine;

L-aspartic acid;

L-citrulline;

L-cysteine-HCl;

L-cystine;

L-glutamic acid;

L-histidine;

Lipoic Acid;

L-isoleucine;

L-leucine;

L-lysine;

L-methionine;

L-ornithine-HCl;

L-phenylalanine;

L-proline;

L-serine;

L-threonine;

L-tryptophan;

L-tyrosine;

L-valine;

Manganese chloride Tetrahydrate;

Niacin;

Nickel dichloride hexahydrate;

Progesterone;

Putrescine 2HCl;

Pyridoxine HCl;

Riboflavin;

Sodium molybdate dehydrate;

Sodium phosphate monobasic;

Sodium selenite;

Thiamine HCl;

Thymidine;

Tin chloride dehydrate;

Uridine;

Vitamin B12;

Vitamin E; and

Zinc sulfate;

to the medium.

2 . The method of claim 1 wherein the final concentration of the components added to the medium from the supplements are about those set forth below:

Adenine sulfate:

1.632

mg/liter

Adenosine:

17.6

mg/liter

Ammonium vanadate:

0.00078

mg/liter

Biotin:

0.28

mg/liter

Choline Chloride:

50.2

mg/liter

Cobalt chloride:

0.0025

mg/liter

Cupric sulfate:

0.0032

mg/liter

Cytidine:

17.6

mg/liter

D-Calcium Pantothenate:

23.8

mg/liter

Ethanolamine HCl:

4.4

mg/liter

Flavin Adenine Dinucleotide:

0.05

mg/liter

Folic Acid:

4.6

mg/liter

Glycine

72

mg/liter

Guanosine:

17.6

mg/liter

Hypoxanthine:

11.8

mg/liter

i-Inositol:

73.2

mg/liter

L-alanine:

8.9

mg/liter

L-arginine

312.4

mg/liter

L-asparagine:

842

mg/liter

L-aspartic acid

97.6

mg/liter

L-citrulline:

12.6

mg/liter

L-cysteine-HCl

224

mg/liter

L-cystine:

34

mg/liter

L-glutamic acid

155.4

mg/liter

L-histidine

167

mg/liter

Lipoic Acid:

0.52

mg/liter

L-isoleucine

422

mg/liter

L-leucine

384

mg/liter

L-lysine

365

mg/liter

L-methionine

147.2

mg/liter

L-ornithine-HCl:

25.6

mg/liter

L-phenylalanine

207

mg/liter

L-proline

239

mg/liter

L-serine:

281

mg/liter

L-threonine

211.6

mg/liter

L-tryptophan

109.2

mg/liter

L-tyrosine

234

mg/liter

L-valine

308.8

mg/liter

Manganese chloride tetrahydrate:

0.0003

mg/liter

Niacin:

31.4

mg/liter

Nickel dichloride hexahydrate:

0.0004

mg/liter

Progesterone:

0.015

mg/liter

Putrescine 2HCl:

0.4

mg/liter

Pyridoxine HCl:

3

mg/liter

Riboflavin:

1.86

mg/liter

Sodium molybdate dehydrate:

0.00016

mg/liter

Sodium phosphate monobasic:

288.2

mg/liter

Sodium selenite:

0.01426

mg/liter

Thiamine HCl:

16

mg/liter

Thymidine:

7.8

mg/liter

Tin chloride dehydrate:

0.00008

mg/liter

Uridine:

17.6

mg/liter

Vitamin B12:

3.4

mg/liter

Vitamin E:

0.376

mg/liter

Zinc sulfate:

1.08

mg/liter

Glucose

1.5

g/liter

L-glutamine

150

mg/liter

3 . The method of claim 1 wherein the supplements are added from an amino acid feed that comprises amino acids at about the following concentrations:

L-arginine:

6.32

g/liter

L-cystine:

1.7

g/liter

L-histidine:

2.1

g/liter

L-isoleucine:

2.6

g/liter

L-leucine:

2.6

g/liter

L-lysine:

3.6

g/liter

L-Methionine:

0.76

g/liter

L-phenylalanine:

1.65

g/liter

L-threonine:

2.38

g/liter

L-tryptophan:

0.51

g/liter

L-tyrosine:

1.8

g/liter

L-valine:

2.34

g/liter

4 . The method of claim 3 wherein about 20 ml amino acid feed is added per liter of culture medium.

5 . The method of claim 1 wherein the supplements are added from an amino acid feed that comprises amino acids at about the following concentrations:

L-alanine:

0.89

g/liter

L-asparagine:

1.5

g/liter

L-aspartic acid:

1.33

g/liter

L-glutamic acid:

1.47

g/liter

Glycine:

0.75

g/liter

L-proline:

1.15

g/liter

L-serine:

1.05

g/liter

6 . The method of claim 5 wherein about 10 ml amino acid feed is added per liter of culture medium.

7 . The method of claim 1 wherein the supplements are added from a nutrient feed that comprises supplements at about the following concentrations:

L-asparagine:

40.6

g/liter

L-proline

10.81

g/liter

L-isoleucine

18.53

g/liter

L-cysteine-HCl

11.19

g/liter

L-leucine

16.58

g/liter

L-threonine

8.2

g/liter

L-tyrosine

9.9

g/liter

L-arginine

9.29

g/liter

L-aspartic acid

3.56

g/liter

L-glutamic acid

6.28

g/liter

Glycine

2.83

g/liter

L-histidine

6.23

g/liter

L-methionine

6.58

g/liter

L-tryptophan

4.93

g/liter

L-lysine

14.66

g/liter

L-phenylalanine

8.64

g/liter

L-valine

13.08

g/liter

L-serine:

13

g/liter

Sodium phosphate Monobasic:

14.41

g/liter

Zinc sulfate:

0.054

g/liter

Cupric sulfate:

0.00016

g/liter

Ammonium vanadate:

0.000039

g/liter

Cobalt chloride:

0.000125

g/liter

Nickel dichloride Hexahydrate:

0.00002

g/liter

Sodium molybdate dehydrate:

0.000008

g/liter

Tin chloride dehydrate:

0.000004

g/liter

Manganese chloride: tetrahydrate:

0.000015

g/liter.

8 . The method of claim 7 wherein about 20 ml nutrient feed is added per liter of culture medium.

9 . The method of claim 1 wherein the supplements are added from a vitamin/salt feed that comprises supplements at about the following concentrations:

Sodium selenite:

7.13 × 10 −4

g/liter

Adenine sulfate:

0.0816

g/liter

Adenosine:

0.88

g/liter

Cytidine:

0.88

g/liter

Guanosine:

0.88

g/liter

Uridine:

0.88

g/liter

Hypoxanthine:

0.59

g/liter

L-citrulline:

0.63

g/liter

L-ornithine-HCl:

1.28

g/liter

Biotin:

0.014

g/liter

Flavin Adenine Dinucleotide:

0.0025

g/liter

Folic Acid:

0.23

g/liter

Lipoic Acid:

0.026

g/liter

Niacin:

1.57

g/liter

Pyridoxine HCl:

0.15

g/liter

Riboflavin:

0.093

g/liter

Thiamine HCl:

0.8

g/liter

Vitamin E:

0.0188

g/liter

Vitamin B12:

0.17

g/liter

Choline Chloride:

2.51

g/liter

Ethanolamine HCl:

0.22

g/liter

i-Inositol:

3.66

g/liter

Thymidine:

0.39

g/liter

Putrescine 2HCl:

0.02

g/liter

Progesterone:

0.00075

g/liter

D-Calcium Pantothenate:

1.19

g/liter

10 . The method of claim 9 wherein about 20 ml vitamin/salt feed is added per liter of culture medium.

11 . The method of claim 1 further comprising harvesting the medium from the host cells; wherein said protein is secreted from said cells into the medium.

12 . The method of claim 13 wherein the culture medium is harvested from the host cells when viability of the cells is below about 60%.

13 . The method of claim 11 further comprising purifying the culture medium from the cells by centrifuging the medium and/or depth filtering the medium and/or filtering the medium through a 0.2 micron filter.

14 . The method of claim 1 wherein the protein is one or more immunoglobulin chains of an antibody or antigen-binding fragment thereof.

15 . The method of claim 14 wherein the antibody or fragment binds specifically to IGF1R.

16 . The method of claim 15 wherein the antibody or fragment comprises a heavy immunoglobulin chain comprising the amino acid sequence set forth in a member selected from the group consisting of SEQ ID NOs: 1, 3,-6, 13, 21 and 26; or a mature fragment thereof or one or more CDRs therefrom; and/or

a light immunoglobulin chain comprising an amino acid sequence selected from the group consisting of SEQ ID NOs: 2, 7-9, 17 and 25, or a mature fragment thereof or one or more CDRs therefrom.

17 . The method of claim 16 wherein the antibody or fragment secreted from the host cell is an antibody that comprises a light chain immunoglobulin comprising amino acids 20-128 of SEQ ID NO: 3, 4, 5, or 6; and a heavy chain immunoglobulin comprising amino acids 20-137 of SEQ ID NO: 8 or 9.

18 . The method of claim 17 wherein the light chain immunoglobulin is linked to a kappa constant immunoglobulin chain and the heavy chain immunoglobulin is linked to a gamma-1 constant immunoglobulin chain.

19 . The method of claim 1 wherein the initial mammalian cell growth medium to which the supplements are added comprises HEPES, sodium bicarbonate buffers, inorganic salts, non-essential amino acids, recombinant human insulin, trace elements and surfactants; and does not comprise L-glutamine, antibiotics, antimycotics or animal-derived components.

20 . A method for producing an antibody comprising inoculating an initial mammalian cell growth medium, pre-warmed to about 37° C.; which initial medium comprises HEPES, sodium bicarbonate buffers, inorganic salts, non-essential amino acids, recombinant human insulin, trace elements and surfactants; and which does not comprise L-glutamine, antibiotics, antimycotics or animal-derived components; with CHO DXB11 host cells expressing the antibody light chain immunoglobulin and heavy chain immunoglobulin, to a cell density of about 2.5-5×10 5 cells/ml; and, adding the following supplements to the medium before, simultaneously with or immediately after said inoculation: soy hydrolysate to a final concentration of about 10 g/liter; and, optionally, an amino acid feed wherein the concentration of the components added by said amino acid feed are approximately those set forth below:

L-arginine:

126.4

mg/liter

L-cystine:

34

mg/liter

L-histidine:

42

mg/liter

L-isoleucine:

52

mg/liter

L-leucine:

52

mg/liter

L-lysine:

72

mg/liter

L-Methionine:

15.2

mg/liter

L-phenylalanine:

33

mg/liter

L-threonine:

47.6

mg/liter

L-tryptophan:

10.2

mg/liter

L-tyrosine:

36

mg/liter

L-valine:

46.8

mg/liter

L-alanine:

8.9

mg/liter

L-asparagine:

30

mg/liter

L-aspartic acid:

26.6

mg/liter

L-glutamic acid:

29.4

mg/liter

glycine:

15

mg/liter

L-proline:

23

mg/liter

L-serine:

21

mg/liter;

and, when viable cell density reaches over about 1.2×10 6 cells/ml, adding supplement feeds wherein the concentration of the components added by said supplement feeds are approximately those set forth below:

Sodium selenite:

0.01426

mg/liter

Adenine sulfate:

1.632

mg/liter

Adenosine:

17.6

mg/liter

Cytidine:

17.6

mg/liter

Guanosine:

17.6

mg/liter

Uridine:

17.6

mg/liter

Hypoxanthine:

11.8

mg/liter

L-citrulline:

12.6

mg/liter

L-ornithine-HCl:

25.6

mg/liter

Biotin:

0.28

mg/liter

Flavin Adenine Dinucleotide:

0.05

mg/liter

Folic Acid:

4.6

mg/liter

Lipoic Acid:

0.52

mg/liter

Niacin:

31.4

mg/liter

Pyridoxine HCl:

3

mg/liter

Riboflavin:

1.86

mg/liter

Thiamine HCl:

16

mg/liter

Vitamin E:

0.376

mg/liter

Vitamin B12:

3.4

mg/liter

Choline Chloride:

50.2

mg/liter

Ethanolamine HCl:

4.4

mg/liter

i-Inositol:

73.2

mg/liter

Thymidine:

7.8

mg/liter

Putrescine 2HCl:

0.4

mg/liter

Progesterone:

0.015

mg/liter

D-Calcium Pantothenate:

23.8

mg/liter

L-asparagine:

812

mg/liter

L-proline

216

mg/liter

L-isoleucine

370

mg/liter

L-cysteine-HCl

224

mg/liter

L-leucine

332

mg/liter

L-threonine

164

mg/liter

L-tyrosine

198

mg/liter

L-arginine

186

mg/liter

L-aspartic acid

71

mg/liter

L-glutamic acid

126

mg/liter

Glycine

57

mg/liter

L-histidine

125

mg/liter

L-methionine

132

mg/liter

L-tryptophan

99

mg/liter

L-lysine

293

mg/liter

L-phenylalanine

174

mg/liter

L-valine

262

mg/liter

L-serine:

260

mg/liter

Sodium phosphate monobasic:

288.2

mg/liter

Zinc sulfate:

1.08

mg/liter

Cupric sulfate:

0.0032

mg/liter

Ammonium vanadate:

0.00078

mg/liter

Cobalt chloride:

0.0025

mg/liter

Nickel dichloride hexahydrate:

0.0004

mg/liter

Sodium molybdate dehydrate:

0.00016

mg/liter;

and, maintaining glucose concentration in the medium at about 1.5 g/liter and maintaining L-glutamine concentration in the medium at about 150 mg/liter; and during cell growth maintaining O 2 concentration at about 60%; pH at about 6.8±0.02 and temperature at about 36.5° C.±0.5° C.; and, optionally, removing the host cells from the medium when cell viability is below about 60%.

21 . The method of claim 20 wherein the antibody comprises a heavy immunoglobulin chain comprising the amino acid sequence set forth in a member selected from the group consisting of SEQ ID NOs: 1, 3,-6, 13, 21 and 26; or a mature fragment thereof or one or more CDRs therefrom; and/or

a light immunoglobulin chain comprising an amino acid sequence selected from the group consisting of SEQ ID NOs: 2, 7-9, 17 and 25, or a mature fragment thereof or one or more CDRs therefrom.

22 . The method of claim 21 wherein the antibody or fragment comprises an antibody secreted from the host cells that comprises a light chain immunoglobulin comprising amino acids 20-128 of SEQ ID NO: 3, 4, 5, or 6; and a heavy chain immunoglobulin comprising amino acids 20-137 of SEQ ID NO: 8 or 9.

23 . The method of claim 22 wherein the light chain immunoglobulin is linked to a kappa constant immunoglobulin chain and the heavy chain immunoglobulin is linked to a gamma-1 constant immunoglobulin chain.

24 . The method of claim 23 further comprising recovering the culture medium from the cells by disk-stack centrifuging the medium, depth filtering the medium and filtering the medium through a filter with about a 0.2 micron pore size.

25 . The method of claim 24 further comprising purifying the immunoglobulins from the medium by column chromatographic fractionation.

26 . An aqueous liquid cell culture medium comprising:

about 10 g/liter soy hydrolysate,

about 1.5 g/liter glucose,

about 150 mg/liter L-glutamine,

pH of about 6.8±0.02,

HEPES,

Sodium bicarbonate buffers,

Inorganic salts,

Non-essential amino acids,

Recombinant human insulin,

Trace elements,

Surfactants,

an amino acid feed wherein the concentration of the components added by said amino acid feed are approximately those set forth below:

L-arginine:

126.4

mg/liter

L-cystine:

34

mg/liter

L-histidine:

42

mg/liter

L-isoleucine:

52

mg/liter

L-leucine:

52

mg/liter

L-lysine:

72

mg/liter

L-Methionine:

15.2

mg/liter

L-phenylalanine:

33

mg/liter

L-threonine:

47.6

mg/liter

L-tryptophan:

10.2

mg/liter

L-tyrosine:

36

mg/liter

L-valine:

46.8

mg/liter

L-alanine:

8.9

mg/liter

L-asparagine:

30

mg/liter

L-aspartic acid:

26.6

mg/liter

L-glutamic acid:

29.4

mg/liter

Glycine:

15

mg/liter

L-proline:

23

mg/liter

L-serine:

21

mg/liter;

wherein the medium does not comprise antibiotics, antimycotics or animal-derived components.

27 . An aqueous liquid culture medium produced by a process comprising inoculating an initial mammalian cell growth medium, pre-warmed to about 37° C.; which medium comprises HEPES, sodium bicarbonate buffers, inorganic salts, non-essential amino acids, recombinant human insulin, trace elements and surfactants; and which does not comprise L-glutamine, antibiotics, antimycotics or animal-derived components; with CHO DXB11 host cells expressing an antibody light chain immunoglobulin and heavy chain immunoglobulin, to a cell density of about 2.5-5×10 5 cells/ml; and, adding the following supplements to the medium before, simultaneously with or immediately after said inoculation:

soy hydrolysate to a final concentration of about 10 g/liter;

and, optionally, an amino acid feed wherein the concentration of the components added by said amino acid feed are approximately those set forth below:

L-arginine:

126.4

mg/liter

L-cystine:

34

mg/liter

L-histidine:

42

mg/liter

L-isoleucine:

52

mg/liter

L-leucine:

52

mg/liter

L-lysine:

72

mg/liter

L-Methionine:

15.2

mg/liter

L-phenylalanine:

33

mg/liter

L-threonine:

47.6

mg/liter

L-tryptophan:

10.2

mg/liter

L-tyrosine:

36

mg/liter

L-valine:

46.8

mg/liter

L-alanine:

8.9

mg/liter

L-asparagine:

30

mg/liter

L-aspartic acid:

26.6

mg/liter

L-glutamic acid:

29.4

mg/liter

Glycine:

15

mg/liter

L-proline:

23

mg/liter

L-serine:

21

mg/liter;

and, when viable cell density reaches over about 1.2×10 6 cells/ml, adding supplement feeds wherein the concentration of the components added by said supplement feeds are approximately those set forth below:

Sodium selenite:

0.01426

mg/liter

Adenine sulfate:

1.632

mg/liter

Adenosine:

17.6

mg/liter

Cytidine:

17.6

mg/liter

Guanosine:

17.6

mg/liter

Uridine:

17.6

mg/liter

Hypoxanthine:

11.8

mg/liter

L-citrulline:

12.6

mg/liter

L-ornithine-HCl:

25.6

mg/liter

Biotin:

0.28

mg/liter

Flavin Adenine Dinucleotide:

0.05

mg/liter

Folic Acid:

4.6

mg/liter

Lipoic Acid:

0.52

mg/liter

Niacin:

31.4

mg/liter

Pyridoxine HCl:

3

mg/liter

Riboflavin:

1.86

mg/liter

Thiamine HCl:

16

mg/liter

Vitamin E:

0.376

mg/liter

Vitamin B12:

3.4

mg/liter

Choline Chloride:

50.2

mg/liter

Ethanolamine HCl:

4.4

mg/liter

i-Inositol:

73.2

mg/liter

Thymidine:

7.8

mg/liter

Putrescine 2HCl:

0.4

mg/liter

Progesterone:

0.015

mg/liter

D-Calcium Pantothenate:

23.8

mg/liter

L-asparagine:

812

mg/liter

L-proline

216

mg/liter

L-isoleucine

370

mg/liter

L-cysteine-HCl

224

mg/liter

L-leucine

332

mg/liter

L-threonine

164

mg/liter

L-tyrosine

198

mg/liter

L-arginine

186

mg/liter

L-aspartic acid

71

mg/liter

L-glutamic acid

126

mg/liter

Glycine

57

mg/liter

L-histidine

125

mg/liter

L-methionine

132

mg/liter

L-tryptophan

99

mg/liter

L-lysine

293

mg/liter

L-phenylalanine

174

mg/liter

L-valine

262

mg/liter

L-serine:

260

mg/liter

Sodium phosphate monobasic:

288.2

mg/liter

Zinc sulfate:

1.08

mg/liter

Cupric sulfate:

0.0032

mg/liter

Ammonium vanadate:

0.00078

mg/liter

Cobalt chloride:

0.0025

mg/liter

Nickel dichloride hexahydrate:

0.0004

mg/liter

Sodium molybdate dehydrate:

0.00016

mg/liter;

and, maintaining glucose concentration in the medium at about 1.5 g/liter and maintaining L-glutamine concentration in the medium at about 150 mg/liter; and during cell growth maintaining O 2 concentration at about 60%; pH at about 6.8±0.02 and temperature at about 36.5° C.±0.5° C.

28 . The aqueous liquid culture medium of claim 27 wherein the host cells comprise a vector encoding the immunoglobulins of the antibody wherein the antibody is secreted into the medium.

29 . The aqueous liquid culture medium of claim 28 wherein the host cell viability is about 60% or lower and/or wherein host cell growth has proceeded for about 14 to 24 days.

30 . The aqueous liquid culture medium of claim 29 wherein the host cells are removed from the medium.

31 . The aqueous liquid culture medium of claim 30 wherein the host cells are removed from the medium by centrifuging the medium and/or depth filtering the medium and/or filtering the medium through a 0.2 micron filter.

32 . The aqueous liquid culture medium of claim 31 wherein the antibody binds specifically to IGF1R.

33 . The aqueous liquid culture medium of claim 32 wherein the heavy immunoglobulin chain comprises the amino acid sequence set forth in a member selected from the group consisting of SEQ ID NOs: 1, 3,-6, 13, 21 and 26; or a mature fragment thereof or one or more CDRs therefrom;

and a light immunoglobulin chain comprises an amino acid sequence selected from the group consisting of SEQ ID NOs: 2, 7-9, 17 and 25, or a mature fragment thereof or one or more CDRs therefrom.

34 . The aqueous liquid culture medium of claim 33 wherein the antibody or fragment is an antibody that is secreted from the host cell that comprises a light chain immunoglobulin comprising amino acids 20-128 of SEQ ID NO: 3, 4, 5, or 6; and a heavy chain immunoglobulin comprising amino acids 20-137 of SEQ ID NO: 8 or 9.

35 . The aqueous liquid culture medium of claim 34 wherein the light chain immunoglobulin is linked to a kappa constant immunoglobulin chain and the heavy chain immunoglobulin is linked to a gamma-1 constant immunoglobulin chain.

36 . A vessel comprising the aqueous liquid culture medium of claim 27 .

37 . The vessel of claim 36 which is a flask, a bioreactor, a tank bioreactor, a bag bioreactor or a disposable bioreactor.

38 . The vessel of claim 37 which bioreactor is a stirred tank bioreactor, a bubble column bioreactor, an air lift bioreactor, a fluidized bed bioreactor or a packed bed bioreactor.

Assignments (1)
CHANGE OF NAME Recorded Aug 30, 2012
From: SCHERING CORPORATION
To: MERCK SHARP & DOHME CORP.
Reel/Frame 028884/0151 →