Abstract: A method for purifying a biologically active substance from a solution mixture containing impurities and the biologically active substance, in which an ion exchange chromatography carrier comprising a matrix and a copolymer containing at least N-isopropylacrylamide as a monomer unit and immobilized to a surface of the matrix is used, and the solution mixture is allowed to flow through a container storing the carrier at a uniform temperature, thereby recovering the biologically active substance.

Abstract: The present invention provides a cation-exchange chromatographic support, comprising a membrane matrix and a copolymer immobilized on the surface of the membrane matrix, wherein the copolymer comprises a (meth)acrylamide-based compound and/or a (meth)acrylate-based compound as monomer units, and the support has one or more species of cation-exchange groups including at least a weak cation-exchange group at a density higher than 30 mmol/L per volume of the support.

Abstract: The present invention provides a cation-exchange chromatographic support, comprising a membrane matrix and a copolymer immobilized on the surface of the membrane matrix, wherein the copolymer comprises a (meth)acrylamide-based compound and/or a (meth)acrylate-based compound as monomer units, and the support has one or more species of cation-exchange groups including at least a weak cation-exchange group at a density higher than 30 mmol/L per volume of the support.

Abstract: Provided is a temperature responsive adsorbent prepared by immobilizing a copolymer containing at least N-isopropylacrylamide to a base material surface. The copolymer has at least a strong cation exchange group. In addition, the copolymer contains the strong cation exchange group in an amount of 0.01 to 5 mol % relative to N-isopropylacrylamide in terms of monomer.

Abstract: Provided is a temperature responsive adsorbent prepared by immobilizing a copolymer containing at least N-isopropylacrylamide to a base material surface. The copolymer has at least a strong cation exchange group. In addition, the copolymer contains the strong cation exchange group in an amount of 0.01 to 5 mol % relative to N-isopropylacrylamide in terms of monomer.

Abstract: A method for purifying a biologically active substance from a solution mixture containing impurities and the biologically active substance, in which an ion exchange chromatography carrier comprising a matrix and a copolymer containing at least N-isopropylacrylamide as a monomer unit and immobilized to a surface of the matrix is used, and the solution mixture is allowed to flow through a container storing the carrier at a uniform temperature, thereby recovering the biologically active substance.

Abstract: A method for manufacturing a high-affinity antibody including purifying an antibody to which a treatment of reducing the affinity for an antigen is not applied by a temperature responsive protein A medium, in which dissociation constant (KD value) to an antigen is smaller than the KD value of an antibody purified by an acid elution type protein A medium.

Abstract: There is provided a method for purifying an antibody using temperature-responsive Protein A, wherein different buffer solutions are used in a washing step of washing a stationary phase having the temperature-responsive Protein A and in an elution step of eluting the antibody captured by the stationary phase, the method including the washing step of washing the stationary phase using a buffer solution at a temperature at which the temperature-responsive Protein A and the antibody are bound and having a first salt concentration, and the elution step of eluting the antibody captured by the stationary phase using a buffer solution at a temperature at which the antibody is released from the temperature-responsive Protein A and having a second salt concentration lower than the first salt concentration.

Abstract: It is an object of the present invention to provide an affinity chromatographic adsorbent using temperature-responsive protein A, wherein the adsorbent is capable of improving the culture productivity of the temperature-responsive protein A and the stability of the temperature-responsive protein A in cell disruption solution. According to the present invention, there is provided an adsorbent consisting of a carrier, to which a polypeptide comprising a tag peptide, a linker sequence, and a B-domain mutant derived from protein A from the N-terminal side thereof binds, wherein the linker sequence is an amino acid sequence that does not comprise a Val-Pro-Arg sequence and is composed of 7 to 12 amino acid residues; and the binding property of the B-domain mutant derived from protein A to an immunoglobulin can vary depending on temperature under conditions of pH 5 to 9 and a temperature of lower than 60° C.

Abstract: Provided is a temperature responsive adsorbent prepared by immobilizing a copolymer containing at least N-isopropylacrylamide to a base material surface. The copolymer has at least a strong cation exchange group. In addition, the copolymer contains the strong cation exchange group in an amount of 0.01 to 5 mol % relative to N-isopropylacrylamide in terms of monomer.

Abstract: A method for manufacturing a carrier having temperature responsive protein A, which is protein A mutated such that a binding property to an antibody changes depending upon temperature, immobilized thereto, wherein the temperature responsive protein A has the binding property to the antibody in a first temperature region and no binding property to the antibody in a second temperature region; and the method comprises a step of immobilizing the temperature responsive protein A to a carrier surface at a temperature within the first temperature region in which the temperature responsive protein A has the binding property to the antibody.

Abstract: Provided is a temperature responsive adsorbent prepared by immobilizing a copolymer containing at least N-isopropylacrylamide to a base material surface. The copolymer has at least a strong cation exchange group. In addition, the copolymer contains the strong cation exchange group in an amount of 0.01 to 5 mol % relative to N-isopropylacrylamide in terms of monomer.

Abstract: A heat resistant microporous membrane containing a thermoplastic resin having a crystalline melting point of 140-300° C. and having a layer structure formed in the direction of membrane thickness, said layer structure containing 5-100% of a layer defined by the following (A) and 95-0% of a layer defined by the following (B): (A) a layer in which the micropores are intra-spherulitic voids, and (B) a layer in which the micropores are intra-spherulitic voids and inter-spherulitic voids.

Abstract: A hydrophilic microporous membrane comprising a thermoplastic resin, having been subjected to hydrophilizing treatment and having a maximum pore size of 0 to 100 nm, wherein when 3 wt % bovine immunoglobulin having a monomer ratio of 80 wt % or more is filtered at a constant pressure of 0.3 MPa, an average permeation rate (liter/m2/h) for 5 minutes from the start of filtration (briefly referred to as globulin permeation rate A) satisfies the following formula (1) and an average permeation rate (liter/m2/h) for 5 minutes from the time point of 55 minutes after the start of filtration (briefly referred to as globulin permeation rate B) satisfies the following formula (2): Globulin permeation rate A>0.0015 ×maximum pore size (nm)2.75 ??(1) Globulin permeation rate B/globulin permeation rate A>0.2 .

Abstract: A multilayer microporous membrane containing a thermoplastic resin, comprising a coarse structure layer with a higher open pore ratio and a fine structure layer with a lower open pore ratio, wherein said coarse structure layer is present at least in one membrane surface having a thickness of not less than 5.0 ?m, a thickness of said fine structure layer is not less than 50% of the whole membrane thickness, and said coarse structure layer and said fine structure layer are formed in one-piece.

Abstract: A hydrophilic microporous membrane comprising a thermoplastic resin, having been subjected to hydrophilizing treatment and having a maximum pore size of 10 to 100 nm, wherein when 3 wt % bovine immunoglobulin having a monomer ratio of 80 wt % or more is filtered at a constant pressure of 0.3 MPa, an average permeation rate (liter/m2/h) for 5 minutes from the start of filtration (briefly referred to as globulin permeation rate A) satisfies the following formula (1) and an average permeation rate (liter/m2/h) for 5 minutes from the time point of 55 minutes after the start of filtration (briefly referred to as globulin permeation rate B) satisfies the following formula (2): Globulin permeation rate A>0.0015×maximum pore size (nm)2.75 ??(1) Globulin permeation rate B/globulin permeation rate A>0.2 ??(2).

Abstract: A multilayer microporous membrane containing a thermoplastic resin, comprising a coarse structure layer with a higher open pore ratio and a fine structure layer with a lower open pore ratio, wherein said coarse structure layer is present at least in one membrane surface having a thickness of not less than 5.0 &mgr;m, a thickness of said fine structure layer is not less than 50% of the whole membrane thickness, and said coarse structure layer and said fine structure layer are formed in one-piece.