Charge-reversed silica sol
AssigneeNouryon Chemicals International B.V.
InventorAnders TÖRNCRONA
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AssigneeNouryon Chemicals International B.V.
InventorAnders TÖRNCRONA
Estimating the term…
A process for producing a charge-reversed aqueous silica sol includes: (a) providing a slurry of an acidic cation-exchange solid in an aqueous liquid; (b) providing a starting aqueous silica sol with an alkaline pH and including a monovalent cation(s); (c) contacting the slurry with the starting sol; (d) separating the acidic cation-exchange solid from the mixture (c) to leave a decationised aqueous silica sol with an acidic pH and a reduced monovalent cation(s) content compared to the starting sol; and (e) contacting the decationised sol with a compound(s) including a modifying element(s) that can adopt a +3 or +4 oxidation state to produce a charge-reversed aqueous silica sol whose silica particles include the modifying element(s) on their surface. The S-value of the starting sol is from about 10 to about 50%, and the surface area of colloidal silica particles in the starting sol is at least about 500 m2 g−1.
A process for producing a charge-reversed aqueous silica sol comprising the steps of:
A charge-reversed aqueous silica sol comprising silica sol particles whose surface is modified with one or more modifying elements capable of adopting a +3 or +4 oxidation state, wherein the amount of the one or more modifying elements on the colloidal silica particles in the charge-reversed aqueous silica sol compared to the surface area of the starting colloidal silica particles is from about 18.4 to about 33 μmol m−2, the charge-reversed silica sol being obtainable by modifying a starting aqueous silica sol with the one or more modifying elements, wherein the starting aqueous silica sol has an S-value of from about 10 to about 50%, and the surface area of the starting aqueous colloidal silica particles is at least about 500 m2 g−1.
Dependencies are inferred from the claim text.