Mary Chen - Burlingame CA, US Lawrence Forman - Sunnyvale CA, US
Assignee:
Genentech, Inc. - South San Francisco CA
International Classification:
C12N005/02
US Classification:
435/325000, 435/383000
Abstract:
A method-of producing a polypeptide in fed batch cell culture is provided which involves an initial cell growth phase and a distinct production phase. In the initial growth stage, animal cells having nucleic acid encoding the polypeptide are cultured at a starting osmolality of about 280-330 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0.01 and 1 g/L. This is followed by a production phase, where the cultured animal cells of the growth phase are inoculated at a cell seed density of at least 1.0×10cells/mL and the cells are cultured at a starting osmolarity of about 400-600 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0.01 and 1 g/L. Preferably, the glutamine concentration in the cell culture medium is simultaneously controlled in order to curtail production of lactic acid and ammonia which result from unnecessarily high glutamine concentrations. During the growth phase, production of potentially detrimental metabolic waste products, such as lactic acid, is controlled thereby curtailing the increase of osmolality due to accumulation and neutralization of waste products. Thus, the cell growth can be improved. In the production phase, the cell culture conditions are modified in order to arrest or reduce cell growth and thereby direct nutrient utilization toward production, as opposed to cell growth. Overall, it is intended that the method results in an improvement in specific productivity, reduction in production run times and/or an increase in final product concentration.
Mary Chen - Burlingame CA, US Lawrence Forman - Sunnyvale CA, US
Assignee:
Genentech, Inc. - South San Francisco CA
International Classification:
C12P021/06 C12N005/06
US Classification:
435069100, 435358000, 435320100
Abstract:
A method of producing a polypeptide in fed batch cell culture is provided which involves an initial cell growth phase and a distinct production phase. In the initial growth stage, animal cells having nucleic acid encoding the polypeptide are cultured at a starting osmolality of about 280-330 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0.01 and 1 g/L. This is followed by a production phase, where the cultured animal cells of the growth phase are inoculated at a cell seed density of at least 1.0×10cells/mL and the cells are cultured at a starting osmolarity of about 400-600 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0.01 and 1 g/L. Preferably, the glutamine concentration in the cell culture medium is simultaneously controlled in order to curtail production of lactic acid and ammonia which result from unnecessarily high glutamine concentrations. During the growth phase, production of potentially detrimental metabolic waste products, such as lactic acid, is controlled thereby curtailing the increase of osmolality due to accumulation and neutralization of waste products. Thus, the cell growth can be improved. In the production phase, the cell culture conditions are modified in order to arrest or reduce cell growth and thereby direct nutrient utilization toward production, as opposed to cell growth. Overall, it is intended that the method results in an improvement in specific productivity, reduction in production run times and/or an increase in final product concentration.
Mary Chen - Burlingame CA Lawrence W. Forman - Sunnyvale CA
Assignee:
Genentech, Inc. - South San Francisco CA
International Classification:
C12N 500 C12N 506
US Classification:
435358
Abstract:
A method of producing a polypeptide in fed batch cell culture is provided which involves an initial cell growth phase and a distinct production phase. In the initial growth stage, animal cells having nucleic acid encoding the polypeptide are cultured at a starting osmolality of about 280-330 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0. 01 and 1 g/L. This is followed by a production phase, where the cultured animal cells of the growth phase are inoculated at a cell seed density of at least 1. times. 10. sup. 6 cells/mL and the cells are cultured at a starting osmolarity of about 400-600 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0. 01 and 1 g/L. Preferably, the glutamine concentration in the cell culture medium is simultaneously controlled in order to curtail production of lactic acid and ammonia which result from unnecessarily high glutamine concentrations.
Mary Chen - Burlingame CA Lawrence W. Forman - Sunnyvale CA
Assignee:
Genentech, Inc. - South San Francisco CA
International Classification:
C12N 500 C12P 2106 C12P 2102 C12P 2104
US Classification:
435325
Abstract:
A method of producing a polypeptide in fed batch cell culture is provided which involves an initial cell growth phase and a distinct production phase. In the initial growth stage, animal cells having nucleic acid encoding the polypeptide are cultured at a starting osmolality of about 280-330 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0. 01 and 1 g/L. This is followed by a production phase, where the cultured animal cells of the growth phase are inoculated at a cell seed density of at least 1. times. 10. sup. 6 cells/mL and the cells are cultured at a starting osmolarity of about 400-600 mOsm in the presence of a concentration of glucose controlled throughout the culturing to be within a range between about 0. 01 and 1 g/L. Preferably, the glutamine concentration in the cell culture medium is simultaneously controlled in order to curtail production of lactic acid and ammonia which result from unnecessarily high glutamine concentrations.
Hybrid Yeast Cell Lines For High Level Production Of Recombinant Protein
- San Mateo CA, US Lawrence Forman - San Mateo CA, US
Assignee:
CHO Plus, Inc. - San Mateo CA
International Classification:
C12N 15/10 C12N 5/16 C12N 15/02 C12N 5/071
Abstract:
This disclosure provides improved cell lines for manufacture of protein, considerably reducing the cost of commercial production. The cell lines are obtained by selecting cells from a mixed population for one or more characteristics that support protein production on a non-specific basis, such as the level of endoplasmic reticulum, Golgi apparatus, and/or other desired phenotypic features, compared with other cells in the starting mixture. Particularly effective producer cell lines can be obtained by preparing the cells for functional selection by making cell hybrids. A gene encoding a heterologous protein of interest may be transfected into the cells before or after one or more cycles of fusion and selection. Depending on the protein product being expressed, cell lines may be obtained that produce eight grams or more of protein per liter of culture fluid.
- San Mateo CA, US Lawrence Forman - San Mateo CA, US
Assignee:
CHO Plus, Inc. - San Mateo CA
International Classification:
C12N 15/10 C12N 5/16 C12N 15/02 C12N 5/071
Abstract:
This disclosure provides improved cell lines for manufacture of protein, considerably reducing the cost of commercial production. The cell lines are obtained by selecting cells from a mixed population for one or more characteristics that support cell growth, compared with other cells in the starting mixture. Particularly effective producer cell lines can be obtained by preparing the cells for functional selection by making cell hybrids. A gene encoding a therapeutic protein of interest may be transfected into the cells before or after one or more cycles of fusion and selection. Depending on the protein product being expressed, cell lines may be obtained that produce eight grams or more of protein per liter of culture fluid.
Cell Lines For High Level Production Of Protein-Based Pharmaceuticals
- San Mateo CA, US Lawrence Forman - San Mateo CA, US
Assignee:
CHO Plus, Inc. - San Mateo CA
International Classification:
C12N 15/10 C12N 5/071 C12N 15/02 C12N 5/16
Abstract:
This disclosure provides improved cell lines for manufacture of protein-based pharmaceutical agents, considerably reducing the cost of commercial production. The cell lines are obtained by selecting cells from a mixed population for one or more characteristics that support protein production on a non-specific basis, such as the level of endoplasmic reticulum, Golgi apparatus, and/or other desired phenotypic features, compared with other cells in the starting mixture. Particularly effective producer cell lines can be obtained by preparing the cells for functional selection by making cell hybrids. A gene encoding a therapeutic protein of interest may be transfected into the cells before or after one or more cycles of fusion and selection. Depending on the protein product being expressed, cell lines may be obtained that produce eight grams or more of protein per liter of culture fluid.
Dr. Forman graduated from the Des Moines University College of Osteopathic Medicine in 1968. He works in Cherry Hill, NJ and specializes in Family Medicine. Dr. Forman is affiliated with Kennedy Health System Cherry Hill.
Name / Title
Company / Classification
Phones & Addresses
Lawrence W. Forman President
Cho Plus, Inc Commercial Physical Research
1241 W Hillsdale Blvd, San Mateo, CA 94403 953 Indiana St, San Francisco, CA 94107
Lawrence Ted Forman
THE NATURE'S HAVEN PARTNERS, LIMITED PARTNERSHIP
Lawrence F. Forman Chief Financial Officer
Technology System Integrator Computer & Network Security · Computer Systems Design · Accountant · Computer Repair · Computer Sales
252 W 38 SUITE 505, New York, NY 10018 (212)9377874, (800)2141874