US4034020A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Graft copolymer preparation
Assignee: International Synthetic Rubber Co Ltd
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Filing: 1976-02-12
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Granted: 1977-07-05
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Expires: 1996-02-12
Abstract
Abstract The invention relates to a continuous flow process for the preparation of graft copolymers, for example ABS, wherein a mixture of a polybutadiene and/or styrenebutadiene copolymer latex, one or more vinyl aromatic monomers and one or more unsaturated nitrile monomers is continuously supplied to a first stage, graft polymerization is initiated in said first stage, the mixture is continuously removed from the said first stage and supplied to at least a second stage wherein graft polymerization is continued, the temperature in each stage being 50° to 100° C, the conversion of monomers to polymer in the first stage not exceeding 65% by weight, and the overall conversion being at least 80% by weight.
Inventors
- 👤 John David Moore
- 👤 Ian Robert Wheeler
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 07:17
CPC Classifications
C; C08; C08F; C08F279/00; C08F279/02; C08F279/04
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
177 words
A process for preparing a graft copolymer comprising admixing one or more vinyl aromatic monomers and one or more unsaturated nitrile monomers with a latex of a rubbery polymer selected from polybutadiene and butadiene-styrene copolymer, characterised by imbibing the mixture for a period of 30 to 50 minutes at a temperature of from 20° to 90° C. under continuous flow conditions continuously supplying the imbibed mixture to a first stirred reactor, at a temperature (T1) of 70° to 90° C., initiating emulsion graft polymerisation in the presence of a free radical initiator in said first stirred reactor and continuing the polymerisation to effect conversion of 40 to 65% by weight of the monomers at a rate not more than 5% per minute, continuously removing the reaction mixture from said first stirred reactor and supplying it to a second stirred reactor, at a temperature equal to or above T1 but not over 100° C. and further continuing the graft polymerisation in the second stirred reactor whereby to convert at least 80% by weight of the monomers to polymer.
Claim 2
Dependent Claim
177 words
A process for preparing a graft copolymer comprising admixing one or more vinyl aromatic monomers and one or more unsaturated nitrile monomers with a latex of a rubbery polymer selected from polybutadiene and butadiene-styrene copolymer, characterised by imbibing the mixture for a period of 30 to 50 minutes at a temperature of from 20° to 90° C. under continuous flow conditions continuously supplying the imbibed mixture to a first stirred reactor, at a temperature (T1) of 70° to 90° C., initiating emulsion graft polymerisation in the presence of a free radical initiator in said first stirred reactor and continuing the polymerisation to effect conversion of 40 to 65% by weight of the monomers at a rate not more than 5% per minute, continuously removing the reaction mixture from said first stirred reactor and supplying it to a second stirred reactor, at a temperature equal to or above T1 but not over 100° C. and further continuing the graft polymerisation in the second stirred reactor whereby to convert at least 80% by weight of the monomers to polymer.
Claim 3
Dependent Claim
24 words
A process according to claim 1 wherein the solids content of latex-monomer mixture is 20 to 35% and there is present an anionic emulsifier.
Claim 4
Dependent Claim
18 words
A process according to claim 2 wherein the solids content of the latex-monomer mixture is 25 to 30%.
Claim 5
Dependent Claim
13 words
A process according to claim 2 wherein the imbibing time is 30 minutes.
Claim 6
Dependent Claim
112 words
A process according to claim 1 wherein the latex is a polybutadiene latex having particles of number average particle diameter (Dn) of at least 1500 A and of weight average particle diameter (Dw) of at least 2500 A and prepared by a process comprising: (1) preparing an aqueous emulsion of butadiene containing 0.5 to 1.5 parts by weight of an anionic emulsifier per hundred parts of butadiene and in addition a thermally-decomposable free radical initiator, (2) initiating polymerization and allowing polymerization to proceed under conditions such that the temperature of the reaction mixture is in excess of 85° C. for at least a part of the reaction, and (3) recovering the latex.
Claim 7
Dependent Claim
24 words
A process according to claim 1 wherein the heat of the polymerization is retained in the reaction mixture in the first and second reactors.
Claim 8
Dependent Claim
42 words
A process according to claim 1 wherein the vinyl aromatic monomer is styrene or alpha methyl styrene and the unsaturated nitrile monomer is acrylonitrile or methacrylonitrile and the ratio of vinyl aromatic monomer to unsaturated nitrile monomer is from 3:1 to 1:1.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-07-04 | 1981-01-03 | 1981-07-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-07-04 | 1985-01-03 | 1985-07-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-07-04 | 1989-01-03 | 1989-07-05 | $7700.00 | Window Closed / Lapsed |