Glycidol functionalized anion exchange stationary phases
US-9486799-B2 · Nov 8, 2016 · US
US9545627B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9545627-B2 |
| Application number | US-201214363919-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 12, 2012 |
| Priority date | Dec 15, 2011 |
| Publication date | Jan 17, 2017 |
| Grant date | Jan 17, 2017 |
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A method for producing a protein adsorbent comprising a substrate and a molecular chain fixed on the surface of the substrate is disclosed. The method comprises, in this order: a dry-heat treatment step of heating a pretreatment adsorbent comprising the substrate and the molecular chain fixed on the surface of the substrate, in which the molecular chain contains a weak electrolytic ion-exchange group; and a wet-heat treatment step of heating the pretreatment adsorbent in a moistened state with a liquid or steam to obtain the protein adsorbent.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a protein adsorbent comprising a substrate and a molecular chain fixed to a surface of the substrate, the method comprising, in this order: a dry-heat treatment step of heating a pretreatment adsorbent comprising the substrate and the molecular chain fixed on the surface of the substrate, the molecular chain comprising a weak electrolytic ion-exchange group; and a wet-heat treatment step of heating the dry-heated adsorbent in a moistened state with a liquid selected from pure water, a buffer solution, an inorganic salt aqueous solution, and a buffer solution comprising an inorganic salt, or steam thereof, and wherein the moistened state of the protein adsorbent is maintained after the wet-heat treatment step to obtain the protein adsorbent. 2. The method according to claim 1 , further comprising a molecular chain forming step of fixing the molecular chain on the surface of the substrate before the dry-heat treatment step. 3. The method according to claim 1 , wherein a dynamic adsorption capacity of bovine serum albumin or lysozyme of the protein adsorbent is 5 mg/mL or more. 4. The method according to claim 1 , wherein the dry-heat treatment step comprises heating the pretreatment adsorbent at 40° C. to 130° C. for 1 hour or more. 5. The method according to claim 1 , wherein the wet-heat treatment step comprises heating the pretreatment adsorbent at 40 to 120° C. for 30 minutes or more in the moistened state.
obtained otherwise than by reactions only involving unsaturated carbon-to-carbon bonds · CPC title
in the weakly basic form · CPC title
Resulting in a chemical bond between the coating or impregnating layer and the carrier, support or substrate, e.g. a covalent bond · CPC title
Fibres or filaments (fibres or filaments in the form of membranes B01J20/28038; B01J20/28007 takes precedence) · CPC title
Affinity chromatography or related techniques based upon selective absorption processes · CPC title
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