US4085267A
Expired / Lapsed
US
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Process for the suspension polymerization of vinyl chloride with low polymer buildup
Assignee: Geon Co
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Filing: 1976-02-23
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Granted: 1978-04-18
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Expires: 1996-02-23
Abstract
Abstract The invention relates to reduction of polymer buildup during the suspension polymerization of vinyl chloride, either alone or with other olefinically unsaturated monomers copolymerizable therewith. There is employed a particular combination of ingredients in the polymerization recipe, the essential features being the use of a water phase inhibitor and an oil phase inhibitor along with a substantially water-insoluble polymerization initiator and operating at a high pH. A multiplicity of charges may be polymerized in the reactor without opening the same.
Inventors
- 👤 Marion George Morningstar
- 👤 Robert Lewis Bowles
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 21:39
CPC Classifications
C; C08; C08F; C08F14/00; C08F14/02; C08F14/04; C08F14/06
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
248 words
A process for preparing vinyl chloride polymer products with substantially no polymer buildup in the reactor which comprises contacting in an aqueous medium in a reactor a mixture comprising (a) vinyl chloride monomer or a mixture thereof with up to about 80% by weight of one or more vinylidene monomers having at least one terminal CH 2 ═C< grouping; (b) a dispersant for the monomer(s); (c) from about 0.0005 weight part to about 0.02 weight part, based on 100 weight parts of monomer(s) of a water-soluble inhibitor in an aqueous caustic solution, said inhibitor being selected from borohydrides having the formula ##STR2## wherein X is an alkali metal and wherein each of R, R' and R" may be hydrogen, phenyl, an alkyl group containing from 1 to 10 carbon atoms, or an alkoxy radical containing from 1 to 10 carbon atoms; and alkali metal nitrites, alkaline earth nitrites, or ammonium nitrite; (d) an oil-soluble, spirit-soluble nigrosine; (e) from about 0.001% by weight to about 1.0% by weight based on the weight of the monomer(s) of an oil-soluble, substantially water-insoluble free radical producing catalyst selected from dialkylperoxydicarbonates wherein the alkyl groups are straight chained or branched and contain from 4 to 14 carbon atoms, adjusting and maintaining the pH of said mixture greater than 7.0, and reacting said mixture at a temperature in the range of about 0° C. to about 100° C. and maintaining the pressure in the range of about 1 to 15 atmospheres throughout the reaction.
Claim 2
Dependent Claim
248 words
A process for preparing vinyl chloride polymer products with substantially no polymer buildup in the reactor which comprises contacting in an aqueous medium in a reactor a mixture comprising (a) vinyl chloride monomer or a mixture thereof with up to about 80% by weight of one or more vinylidene monomers having at least one terminal CH 2 ═C< grouping; (b) a dispersant for the monomer(s); (c) from about 0.0005 weight part to about 0.02 weight part, based on 100 weight parts of monomer(s) of a water-soluble inhibitor in an aqueous caustic solution, said inhibitor being selected from borohydrides having the formula ##STR2## wherein X is an alkali metal and wherein each of R, R' and R" may be hydrogen, phenyl, an alkyl group containing from 1 to 10 carbon atoms, or an alkoxy radical containing from 1 to 10 carbon atoms; and alkali metal nitrites, alkaline earth nitrites, or ammonium nitrite; (d) an oil-soluble, spirit-soluble nigrosine; (e) from about 0.001% by weight to about 1.0% by weight based on the weight of the monomer(s) of an oil-soluble, substantially water-insoluble free radical producing catalyst selected from dialkylperoxydicarbonates wherein the alkyl groups are straight chained or branched and contain from 4 to 14 carbon atoms, adjusting and maintaining the pH of said mixture greater than 7.0, and reacting said mixture at a temperature in the range of about 0° C. to about 100° C. and maintaining the pressure in the range of about 1 to 15 atmospheres throughout the reaction.
Claim 3
Dependent Claim
23 words
The process of claim 1 wherein the reactor is maintained completely full during the entire reaction by the addition of aqueous medium thereto.
Claim 4
Dependent Claim
11 words
The process of claim 1 wherein vinyl chloride monomer is polymerized.
Claim 5
Dependent Claim
12 words
The process of claim 1 wherein the dispersant is methyl hydroxypropyl cellulose.
Claim 6
Dependent Claim
12 words
The process of claim 1 wherein the water-soluble inhibitor is sodium borohydride.
Claim 7
Dependent Claim
24 words
The process of claim 1 wherein the catalyst is added last to said mixture and after the same is brought to the reaction temperature.
Claim 8
Dependent Claim
11 words
The process of claim 1 wherein the catalyst is di-sec-butyl peroxydicarbonate.
Claim 9
Dependent Claim
11 words
The process of claim 1 wherein the catalyst is di(2-ethylhexyl) peroxydicarbonate.
Claim 10
Dependent Claim
12 words
The process of claim 1 wherein the catalyst is di(4-t-butyl cyclohexyl) peroxydicarbonate.
Claim 11
Dependent Claim
11 words
The process of claim 2 wherein vinyl chloride monomer is polymerized.
Claim 12
Dependent Claim
12 words
The process of claim 10 wherein the catalyst is di(4-t-butyl cyclohexyl) peroxydicarbonate.
Claim 13
Dependent Claim
12 words
The process of claim 11 wherein the dispersant is methyl hydroxypropyl cellulose.
Claim 14
Dependent Claim
12 words
The process of claim 12 wherein the water-soluble inhibitor is sodium borohydride.
Claim 15
Dependent Claim
11 words
The process of claim 13 wherein the oil-soluble inhibitor is nigrosine.
Claim 16
Dependent Claim
23 words
The process of claim 14 wherein the pH of the mixture is maintained in the range of 8.0 to 10.0 throughout the reaction.
Claim 17
Dependent Claim
23 words
The process of claim 1 wherein the pH of the mixture is maintained in the range of 8.0 to 10.0 throughout the reaction.
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) | 1981-04-17 | 1981-10-17 | 1982-04-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-04-17 | 1985-10-17 | 1986-04-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-04-17 | 1989-10-17 | 1990-04-18 | $7700.00 | Window Closed / Lapsed |