Abstract: Methods of protein production in a linked culture and production bioreactor system are provided. Such methods include a culture bioreactor (N-1 bioreactor) linked to production bioreactor (N bioreactor). More specifically, the methods include (a) culturing cells with a gene that encodes the protein of interest in a continuous perfusion culture bioreactor (N-1 bioreactor); inoculating a continuously stirred tank reactor (CSTR) production bioreactor (N bioreactor) with cells obtained from step (a); and culturing the cells in the CSTR production bioreactor under conditions that allow production of the protein of interest.

Abstract: Methods of protein production in continuous perfusion mammalian cell culture bioreactors are provided. Methods for continuous perfusion culture by allowing cells to self-regulate the rate of addition of perfusion medium to the bioreactor via a pH change are presented. Compositions comprising the perfusion medium as well as the process advantages of using hi-end pH control of perfusion or HIPCOP are also presented.

Abstract: Methods of protein production in a linked culture and production bioreactor system are provided. Such methods include a culture bioreactor (N?1 bioreactor) linked to production bioreactor (N bioreactor). More specifically, the methods include (a) culturing cells with a gene that encodes the protein of interest in a continuous perfusion culture bioreactor (N?1 bioreactor); inoculating a continuously stirred tank reactor (CSTR) production bioreactor (N bioreactor) with cells obtained from step (a); and culturing the cells in the CSTR production bioreactor under conditions that allow production of the protein of interest.

Abstract: Methods of protein production in continuous perfusion mammalian cell culture bioreactors are provided. Methods for continuous perfusion culture by allowing cells to self-regulate the rate of addition of perfusion medium to the bioreactor via a pH change are presented. Compositions comprising the perfusion medium as well as the process advantages of using hi-end pH control of perfusion or HIPCOP are also presented.

Abstract: Methods of protein production in continuous perfusion mammalian cell culture bioreactors are provided. Methods for continuous perfusion culture by allowing cells to self-regulate the rate of addition of perfusion medium to the bioreactor via a pH change are presented. Compositions comprising the perfusion medium as well as the process advantages of using hi-end pH control of perfusion or HIPCOP are also presented.

Abstract: Methods of protein production in continuous perfusion mammalian cell culture bioreactors are provided. Methods for continuous perfusion culture by allowing cells to self-regulate the rate of addition of perfusion medium to the bioreactor via a pH change are presented. Compositions comprising the perfusion medium as well as the process advantages of using hi-end pH control of perfusion or HIPCOP are also presented.

Abstract: Methods of protein production in a linked culture and production bioreactor system are provided. Such methods include a culture bioreactor (N?1 bioreactor) linked to production bioreactor (N bioreactor). More specifically, the methods include (a) culturing cells with a gene that encodes the protein of interest in a continuous perfusion culture bioreactor (N?1 bioreactor); inoculating a continuously stirred tank reactor (CSTR) production bioreactor (N bioreactor) with cells obtained from step (a); and culturing the cells in the CSTR production bioreactor under conditions that allow production of the protein of interest.

Abstract: Methods of protein production in a linked culture and production bioreactor system are provided. Such methods include a culture bioreactor (N-1 bioreactor) linked to production bioreactor (N bioreactor). More specifically, the methods include (a) culturing cells with a gene that encodes the protein of interest in a continuous perfusion culture bioreactor (N-1 bioreactor); inoculating a continuously stirred tank reactor (CSTR) production bioreactor (N bioreactor) with cells obtained from step (a); and culturing the cells in the CSTR production bioreactor under conditions that allow production of the protein of interest.

Abstract: Methods of protein production in a linked culture and production bioreactor system are provided. Such methods include a culture bioreactor (N-1 bioreactor) linked to production bioreactor (N bioreactor). More specifically, the methods include (a) culturing cells with a gene that encodes the protein of interest in a continuous perfusion culture bioreactor (N-1 bioreactor); inoculating a continuously stirred tank reactor (CSTR) production bioreactor (N bioreactor) with cells obtained from step (a); and culturing the cells in the CSTR production bioreactor under conditions that allow production of the protein of interest.

Abstract: Methods of protein production in continuous perfusion mammalian cell culture bioreactors are provided. Methods for continuous perfusion culture by allowing cells to self-regulate the rate of addition of perfusion medium to the bioreactor via a pH change are presented. Compositions comprising the perfusion medium as well as the process advantages of using hi-end pH control of perfusion or HIPCOP are also presented.