US4604454A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of recovering vinyl chloride resin
Assignee: Zeon Corp
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Filing: 1984-10-26
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Granted: 1986-08-05
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Expires: 2004-10-26
Abstract
Abstract A method of recovering a vinyl chloride resin, which comprises mixing an aqueous dispersion of a vinyl chloride resin with an organic liquid which is difficultly soluble in water and does not dissolve nor swell the vinyl chloride resin to form a granular aggregate of the vinyl chloride resin, dehydrating the aggregate and drying it, wherein the granular aggregate before dehydration is adjusted to such a particle size that it contains not more than 20% by weight of particles having a particle diameter of not more than 100 microns.
Inventors
- 👤 Masaaki Nishina
- 👤 Shiro Imaizumi
- 👤 Osamu Ozaki
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 07:43
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/12; C08J3/16; C08F; C08F6/00; C08F6/24; C08J2327/00; C08J2327/02; C08J2327/04; C08J2327/06
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
172 words
A method of recovering a vinyl chloride resin in the form of granules having good flow characteristics and suitable for use in paste processing, said method comprising the steps of mixing an aqueous dispersion containing 10-70% by weight of a vinyl chloride resin at a temperature of 20° to 70° C. with from 0.5 to 30 parts by weight, per 100 parts by weight of the vinyl chloride resin in the aqueous dispersion, of an organic liquid which is difficultly soluble in water and does not dissolve nor swell the vinyl chloride resin to form a granular aggregate of the vinyl chloride resin, classifying the granular aggregate by passing the granular aggregate through a sieve to thereby adjust the particle size of the granular aggregate to contain not more than 20% by weight of particles having a particle diameter of not more than 100 microns, and dehydrating and drying the particle size-adjusted granular aggregate to thereby recover said vinyl chloride resin as an easily dispersible, non-agglomerating mass of granules having good flowability.
Claim 2
Independent Claim
172 words
A method of recovering a vinyl chloride resin in the form of granules having good flow characteristics and suitable for use in paste processing, said method comprising the steps of mixing an aqueous dispersion containing 10-70% by weight of a vinyl chloride resin at a temperature of 20° to 70° C. with from 0.5 to 30 parts by weight, per 100 parts by weight of the vinyl chloride resin in the aqueous dispersion, of an organic liquid which is difficultly soluble in water and does not dissolve nor swell the vinyl chloride resin to form a granular aggregate of the vinyl chloride resin, classifying the granular aggregate by passing the granular aggregate through a sieve to thereby adjust the particle size of the granular aggregate to contain not more than 20% by weight of particles having a particle diameter of not more than 100 microns, and dehydrating and drying the particle size-adjusted granular aggregate to thereby recover said vinyl chloride resin as an easily dispersible, non-agglomerating mass of granules having good flowability.
Claim 3
Dependent Claim
35 words
The method of claim 1 wherein the particle size of the granular aggregate is adjusted to contain not more than 10% by weight of particles having a particle diameter of not more than 100 microns.
Claim 4
Dependent Claim
27 words
The method of claim 1 wherein the organic liquid has a melting point of not more than 20° C. and a boiling point above about 200° C.
Claim 5
Dependent Claim
62 words
The method of claim 1 wherein the organic liquid is selected from the group consisting of alkyl phthalate plasticizers, aromatic carboxylate plasticizers, aliphatic dibasic acid ester plasticizers, phosphate plasticizers, aliphatic glycol ester plasticizers, polyester plasticizers, fatty acid ester secondary plasticizers, epoxy secondary plasticizers, chlorinated paraffin secondary plasticizers, aliphatic dibasic acid ester secondary plasticizers, petroleum diluents, long-chain alkyl benzene diluents and liquid lubricants.
Claim 6
Dependent Claim
14 words
The method of claim 1 wherein the organic liquid is an alkyl phthalate plasticizer.
Claim 7
Dependent Claim
23 words
The method of claim 5 wherein the alkyl phthalate plasticizer is dioctyl phthalate, dinonyl phthalate, butyl lauryl phthalate, methyl oleyl phthalate, or di-2-ethylhexylphthalate.
Claim 8
Dependent Claim
36 words
The method of claim 1 wherein the aqueous dispersion is mixed with 1 to 15 parts by weight, per 100 parts by weight of the vinyl chloride resin in the aqueous dispersion, of the organic liquid.
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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) | 1989-08-04 | 1990-02-03 | 1990-08-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-08-04 | 1994-02-03 | 1994-08-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-08-04 | 1998-02-03 | 1998-08-05 | $7700.00 | Window Closed / Lapsed |