US2012322983A1PendingUtilityA1
Method for purifying protein
Est. expiryOct 26, 2027(~1.3 yrs left)· nominal 20-yr term from priority
B01D 71/261B01D 71/34B01D 71/78C07K 1/18B01D 71/82B01D 69/08
47
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Claims
Abstract
The present invention provides a method for purifying a protein to remove impurities from a mixture liquid containing a desired protein and the impurities, comprising performing filtration using a porous membrane having a graft chain on a pore surface and an anion-exchange group fixed to the graft chain.
Claims
exact text as granted — not AI-modified1 . A method for purifying a protein to remove impurities from a mixture liquid containing a desired protein and the impurities, comprising:
performing filtration using a porous membrane having a graft chain on a pore surface and an anion-exchange group fixed to the graft chain.
2 . The method for purifying the protein according to claim 1 , wherein the desired protein is one selected from the group consisting of monoclonal antibodies, polyclonal antibodies, humanized antibodies, human antibodies, and immunoglobulins.
3 . The method for purifying the protein according to claim 1 , wherein the impurities are at least one selected from the group consisting of a non-turbid component and a turbid component dispersed in the mixture liquid.
4 . The method for purifying the protein according to claim 3 , wherein the non-turbid component is at least one selected from the group consisting of impurity proteins, HCP, DNA, viruses, endotoxins, proteases, and bacteria dissolved in the mixture liquid.
5 . The method for purifying the protein according to claim 3 , wherein the turbid component dispersed in the mixture liquid is at least one selected from the group consisting of cells and cell debris.
6 . The method for purifying the protein according to claim 1 , wherein a salt concentration of the mixture liquid is from 0.01 M to 0.5 M (both inclusive).
7 . The method for purifying the protein according to claim 6 , wherein the salt concentration of the mixture liquid is from 0.1 M to 0.3 M (both inclusive).
8 . The method for purifying the protein according to claim 1 , wherein:
a base material of the porous membrane is polyethylene or polyvinylidene fluoride, the graft chain is a polymer of glycidyl methacrylate and has a graft rate of from 10% to 250% (both inclusive), and the graft chain has 70% or more of epoxy groups replaced with the anion-exchange groups.
9 . The method for purifying the protein according to claim 8 , wherein the graft rate is from 10% to 150% (both inclusive).
10 . The method for purifying the protein according to claim 8 , wherein the graft rate is from 10% to 90% (both inclusive).
11 . The method for purifying the protein according to claim 8 , wherein the graft rate is from 30% to 60% (both inclusive).
12 . The method for purifying the protein according to claim 1 , wherein the anion-exchange group is a diethylamino group and/or a trimethylamino group.
13 . The method for purifying the protein according to claim 1 , wherein the anion-exchange group is a diethylamino group.
14 . The method for purifying the protein according to claim 1 , wherein the porous membrane has a maximum pore size of from 0.1 μm to 0.8 μm (both inclusive).
15 . The method for purifying the protein according to claim 1 , wherein the mixture liquid is filtered using the porous membrane to remove one or more impurities comprising a non-turbid component.
16 . The method for purifying the protein according to claim 1 , wherein the mixture liquid is an animal cell culture.
17 . The method for purifying the protein according to claim 1 , wherein the porous membrane is a porous hollow fiber membrane.
18 . The method for purifying a protein according to claim 1 , further comprising performing purification using affinity chromatography.Join the waitlist — get patent alerts
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