US4767803A
Expired / Lapsed
US
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Method of producing coagulated colloidal particles
Assignee: Kanegafuchi Chemical Industry Co Ltd
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Filing: 1986-07-02
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Granted: 1988-08-30
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Expires: 2006-07-02
Abstract
Abstract Disclosed is a method of producing coagulated colloidal particles with close-packed structure which comprises; (A) adding a coagulant to aqueous colloidal particles at a temperature lower than softening temperature of the colloidal particles under such conditions that said coagulant will be present in discrete units in the dispersion before it is brought into solution by diffusion; (B) allowing the molecules of coagulant to gradually diffuse from said coagulant units into the surrounding dispersion, thereby coagulating the colloidal particles on the surface of each coagulant unit, causing the coagulated particles to grow from inside to outside of each unit, and producing coagulated particles of desired size with regularly packed structure; (C) separating the coagulated particles thus formed from the dispersion; and (D) drying, or heating in an aqueous phase, the coagulated particles separated above at a temperature lower than the softening point of said colloidal particles.
Inventors
- 👤 Hideo Yasui
- 👤 Yasuhiro Miki
- 👤 Wataru Okada
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 14:59
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/14; C08F6/22; C08C; C08C1/00; C08C1/14; C08C1/16; Y; Y10; Y10S; Y10S528/00; Y10S528/931; Y10S528/934; Y10S528/936
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
173 words
Method of producing densely packed coagulated colloidal particles which comprises the following steps: (A) adding a coagulant to an aqueous dispersion of primary colloidal particles which can be coagulated by addition of said coagulant, at a temperature lower than the temperature at which said colloidal primary particles begin to fuse, under such conditions that said coagulant is present in discrete coagulant units in the dispersion before said coagulant is brought into solution by diffusion; (B) allowing molecules of coagulant to diffuse from said coagulant units into the surrounding dispersion, thereby causing primary colloidal particles to coagulate on the surface of each coagulant unit and causing the coagulated particles to grow from inside to outside of each unit to produce coagulated particles having a desired size and comprising primary colloidal particles regularly arranged in a crystal-like structure; (C) separating the coagulated particles thus formed from the dispersion; and (D) drying, or heating in an aqueous phase, the coagulated particles separated above at a temperature lower than the softening point of said primary colloidal particles.
Claim 2
Dependent Claim
173 words
Method of producing densely packed coagulated colloidal particles which comprises the following steps: (A) adding a coagulant to an aqueous dispersion of primary colloidal particles which can be coagulated by addition of said coagulant, at a temperature lower than the temperature at which said colloidal primary particles begin to fuse, under such conditions that said coagulant is present in discrete coagulant units in the dispersion before said coagulant is brought into solution by diffusion; (B) allowing molecules of coagulant to diffuse from said coagulant units into the surrounding dispersion, thereby causing primary colloidal particles to coagulate on the surface of each coagulant unit and causing the coagulated particles to grow from inside to outside of each unit to produce coagulated particles having a desired size and comprising primary colloidal particles regularly arranged in a crystal-like structure; (C) separating the coagulated particles thus formed from the dispersion; and (D) drying, or heating in an aqueous phase, the coagulated particles separated above at a temperature lower than the softening point of said primary colloidal particles.
Claim 3
Dependent Claim
55 words
Method of producing spherical, high-density, coagulated colloidal particles comprising primary colloidal particles which are closely and homogeneously packed and comprising no empty space of a size larger than a primary colloidal particle, which comprises heating the dried coagulated particles obtained in claim 1 at a temperature higher than the softening point of the primary particles.
Claim 4
Dependent Claim
16 words
The method as defined in claim 1, wherein said aqueous colloidal particles are a polymer latex.
Claim 5
Dependent Claim
61 words
The method as defined in claim 3, wherein said polymer latex is a latex of a copolymer prepared by copolymerization of a monomer mixture consisting of 20 to 80 parts of acrylonitrile, 20 to 80 parts of at least one member selected from vinyl chloride, vinylidene chloride, vinyl bromide and vinylidene bromide, and 0 to 10 parts of a dyable monomer.
Claim 6
Dependent Claim
35 words
The method as defined in claim 3, wherein said polymer latex is a latex of a butadiene polymer composed of 0 to 50 weight % of styrene and 50 to 100 weight % of butadiene.
Claim 7
Dependent Claim
91 words
The method as defined in claim 5, wherein said polymer latex is a latex of a copolymer prepared by polymerizing 20 to 80 parts of a monomer mixture composed of 0 to 50 weight % of an acrylate, 0 to 100 weight % of a methacrylate, 0 to 90 weight % of an aromatic vinyl monomer, 0 to 90 weight % of a cyano vinyl monomer and 0 to 20 weight % of other copolymerizable monomer, in the presence of 20 to 80 parts of a latex of a butadiene polymer.
Claim 8
Dependent Claim
113 words
The method as defined in claim 3, wherein said polymer latex is a latex of a copolymer prepared by polymerizing 80 to 100 parts of a monomer mixture composed of 0 to 100 weight % of methyl methacrylate, 0 to 60 weight % of an acrylate or a methacrylate other than methyl methacrylate, 0 to 90 weight % of an aromatic vinyl monomer and 0 to 90 weight % of a cyano vinyl monomer, in the presence of 0 to 20 parts of a latex of an elastomer composed of 0 to 50 weight % of styrene, 50 to 100 weight % of butadiene and 0 to 30 weight % of an acrylate.
Claim 9
Dependent Claim
126 words
The method as defined in claim 3, wherein said polymer latex is a mixture of (A) 0 to 50 parts of a latex of a graft copolymer prepared by polymerizing 10 to 90 parts of at least one member selected from aromatic vinyl monomers, methacrylates, acrylates, and cyano vinyl monomers, in the presence of 10 to 90 parts of a butadiene polymer composed of 0 to 50 weight % of styrene and 50 to 100 weight % of butadiene, with (B) 50 to 100 parts of a latex of copolymer composed of 0 to 70 mol % of α-methylstyrene and 30 to 100 mol % of at least one member selected from aromatic vinyl monomers other than α-methylstyrene, methacrylates, acrylates, acrylic acid and cyano vinyl monomers.
Claim 10
Dependent Claim
105 words
The method as defined in claim 3, wherein said polymer latex is a latex of a copolymer prepared by polymerizing 15 to 95 parts of at least one member selected from methacrylates, cyano vinyl monomers, acrylates, aromatic vinyl monomers and other monomers copolymerizable therewith, in the presence of 5 to 85 parts of a latex of an elastomer composed of 40 to 100 weight % of an acrylate, 0 to 60 weight % of at least one member selected from aromatic vinyl monomers, cyano vinyl monomers, vinyl chloride, vinylidene chloride, vinyl acetate and conjugated diolefins, and 0 to 10 weight % of a cross-linkable monomer.
Claim 11
Dependent Claim
58 words
The method as defined in claim 3, wherein said polymer latex is a latex of a copolymer prepared by polymerizing 40 to 100 parts of vinylidene chloride and 0 to 60 parts of at least one member selected from aromatic vinyl monomers, cyano vinyl monomers, acrylates, methacrylates, acrylic acid, methacrylic acid, itaconic acid, maleic acid and cross-linkable monomers.
Claim 12
Dependent Claim
65 words
The method as defined in claim 3, wherein said polymer latex is a latex of a copolymer prepared by polymerizing 40 to 100 parts of vinyl chloride, 0 to 20 parts of a cyano vinyl monomer and 0 to 60 parts of at least one member selected from vinylidene chloride, vinyl bromide, acrylates, methacrylates, acrylic acid, methacrylic acid, itaconic acid, maleic acid and cross-linkable monomers.
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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) | 1991-08-30 | 1992-02-29 | 1992-08-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-08-30 | 1996-02-29 | 1996-08-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-08-30 | 2000-02-29 | 2000-08-30 | $7700.00 | Window Closed / Lapsed |