US4090887A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Pigmented microporous silica microspheres produced by a water in oil emulsion
Assignee: EIDP Inc
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Filing: 1975-11-25
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Granted: 1978-05-23
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Expires: 1995-11-25
Abstract
Abstract Pigmented silica microspheres having an average diameter from 2 μm to 100 μm and consisting essentially of from 10% to 70% by weight of particulate pigment, dispersed throughout a microporous silica matrix and, optionally, containing a coating of dense amorphous silica. The microspheres are produced by acidifying a water-in-oil emulsion. The pigmented silica micropheres are particularly useful as opacifying agents for coating compositions and as fillers for paper.
Inventors
- 👤 Mark James Marquisee
- 👤 Lionel Samuel Sandell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 10:59
CPC Classifications
C; C09; C09C; C09C1/00; C09B; C09B67/00; C09B67/006; C01; C01P; C01P2006/00; C01P2006/12; C01P2006/16; Y; Y10; Y10T; Y10T428/00; Y10T428/29; Y10T428/2982
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
172 words
Process for preparing pigmented silica microspheres by the steps of (i) forming a water-in-oil emulsion by contacting a siliceous aqueous phase with an oil phase, said siliceous aqueous phase consisting of water, particulate pigment, and at least one silicon compound selected from the group consisting of collodial silica and alkali metal silicates, said oil phase consisting of at least one water-immiscible hydrocarbon selected from the group consisting of liquid and low melting aliphatic, aromatic and chlorinated hydrocarbons and from 0.5% to 15% by weight of a nonionic water-in-oil emulsifier, based on the total weight of the oil phase, (ii) adding acid to the water-in-oil emulsion formed in Step (i), the acid being added in an amount from 0.5 to 2.0 times the amount of acid needed to react stoichiometrically with the total amount of base present in the siliceous aqueous phase of Step (i) to gel the siliceous aqueous phase and form a slurry of pigmented silica microspheres, and (iii) separating the pigmented silica microspheres from the slurry formed in Step (ii).
Claim 2
Dependent Claim
172 words
Process for preparing pigmented silica microspheres by the steps of (i) forming a water-in-oil emulsion by contacting a siliceous aqueous phase with an oil phase, said siliceous aqueous phase consisting of water, particulate pigment, and at least one silicon compound selected from the group consisting of collodial silica and alkali metal silicates, said oil phase consisting of at least one water-immiscible hydrocarbon selected from the group consisting of liquid and low melting aliphatic, aromatic and chlorinated hydrocarbons and from 0.5% to 15% by weight of a nonionic water-in-oil emulsifier, based on the total weight of the oil phase, (ii) adding acid to the water-in-oil emulsion formed in Step (i), the acid being added in an amount from 0.5 to 2.0 times the amount of acid needed to react stoichiometrically with the total amount of base present in the siliceous aqueous phase of Step (i) to gel the siliceous aqueous phase and form a slurry of pigmented silica microspheres, and (iii) separating the pigmented silica microspheres from the slurry formed in Step (ii).
Claim 3
Dependent Claim
45 words
Process for preparing pigmented silica microspheres according to claim 1 wherein in Step (i) the amount of silica in the siliceous aqueous phase is from 5% to 40% by weight, calculated as SiO 2 and based on the total weight of the siliceous aqueous phase.
Claim 4
Dependent Claim
44 words
Process for preparing pigmented silica microspheres according to claim 2 wherein in Step (i) the amount of particulate pigment in the siliceous aqueous phase is from 10% to 70% by weight, based on the total weight of the solids in the siliceous aqueous phase.
Claim 5
Dependent Claim
38 words
Process for preparing pigmented silica microspheres according to claim 3 wherein in Step (i) the ratio of the total volume of the siliceous aqueous phase to the total volume of the oil phase is from 1:6 to 1:1.
Claim 6
Dependent Claim
53 words
Process for preparing pigmented silica microspheres according to claim 4 comprising the additional steps of (iva) forming an aqueous slurry of pigmented silica microspheres of Step (iii), and (va) heating the aqueous slurry of Step (iv) at a temperature from 80° C. to 300° C. and at a pH from 5 to 10.7.
Claim 7
Dependent Claim
22 words
Process for preparing pigmented silica microspheres according to claim 5 wherein the silicon compound of Step (i) is an alkali metal silicate.
Claim 8
Dependent Claim
149 words
Process for preparing pigmented silica microspheres according to claim 4 comprising the additional steps of (iv) forming an aqueous slurry of pigmented silica microspheres, (v) adjusting the pH of the aqueous slurry of Step (iv) to from 8 to 11 at a temperature from 60° C. to 125° C., (vi) contacting the aqueous slurry of Step (v) with an aqueous solution of an alkali metal silicate in an amount sufficient to provide from 2% to 40% by weight of silica, calculated as SiO 2 and based on the total solids in the aqueous slurry of Step (v) and the aqueous solution, (vii) adjusting the pH of the slurry of Step (vi) to less than 8 to deposit a coating of dense amorphous silica on the pigmented silica microspheres, and (viii) maintaining the slurry of Step (vii) at a temperature of at least 80° C. for at least 1 hour.
Claim 9
Dependent Claim
20 words
Process for preparing pigmented silica microspheres according to claim 7 wherein in Step (i) the silicon compound is colloidal silica.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-05-22 | 1981-11-21 | 1982-05-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-05-22 | 1985-11-21 | 1986-05-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-05-22 | 1989-11-21 | 1990-05-23 | $7700.00 | Window Closed / Lapsed |