US4074035A
Expired / Lapsed
US
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Halomethylated aromatic interpolymers
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1975-04-22
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Granted: 1978-02-14
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Expires: 1995-04-22
Abstract
Abstract A continuous process for the preparation of gel-free interpolymers from monomers comprising one or more halomethylated vinyl aromatic compounds and one or more Type III monoolefins is characterized by the use of a solvent or mixture of solvents in which the reactants and the interpolymers are soluble; a soluble Lewis acid or Friedel-Crafts catalyst, especially an organo-Group IIIa element halide catalyst; a reaction temperature in the range of -120 DEG C to -20 DEG C; and a conversion of at least one of the monomers to interpolymer in excess of 85 percent. The interpolymers may be crosslinked with nucleophilic reagents to produce elastomeric compositions; quaternized with nitrogen, sulfur or phosphorous compounds to give self-emulsifying latices useful as surface coatings or converted to sulfonic or carboxylic derivatives for the preparation of ionomer resins. The interpolymers are also versatile intermediates which enable the preparation by simple substitution reactions of a wide range of functional-group containing elastomers especially useful in adhesive applications, and as flexibilizers for brittle functional-group containing plastics such as epoxies and amino resins.
Inventors
- 👤 Kenneth W. Powers
- 👤 Irving Kuntz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 21:43
CPC Classifications
C; C08; C08F; C08F212/00; C08F212/02; C08F212/04; C08F212/06; C08F212/12; C08F210/00; C08F210/04; C08F210/08; C08F210/10; C08F8/00; Y; Y10; Y10S; Y10S260/00; Y10S260/31
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
177 words
A continuous process for the preparation of gel-free interpolymers comprised of isobutylene and a mixture of from 0.5 to 5.0 mol % meta and para chloromethyl styrene which comprises: (a) continuously feeding said monomers in the range of about 2 to about 20 parts by weight, about 80 to about 98 parts by weight of a solvent or mixture of solvents in which said monomers and said interpolymers are soluble and from about 0.001 to about 0.05 parts by weight of a catalyst selected from the group consisting of ethyl aluminum dichloride, ethyl aluminum sesquichloride, diethyl aluminum chloride, or boron trifluoride to a reaction zone maintained at a temperature in the range of about -120° C. to about -20° C. to form a reaction mixture; (b) maintaining said reaction mixture in said reaction zone at said temperature for a time sufficient to convert at least one of said monomers to said interpolymer in an amount equal to or greater than about 85 percent; and (c) recovering said interpolymer from the effluent reaction mixture leaving said reaction zone.
Claim 2
Dependent Claim
177 words
A continuous process for the preparation of gel-free interpolymers comprised of isobutylene and a mixture of from 0.5 to 5.0 mol % meta and para chloromethyl styrene which comprises: (a) continuously feeding said monomers in the range of about 2 to about 20 parts by weight, about 80 to about 98 parts by weight of a solvent or mixture of solvents in which said monomers and said interpolymers are soluble and from about 0.001 to about 0.05 parts by weight of a catalyst selected from the group consisting of ethyl aluminum dichloride, ethyl aluminum sesquichloride, diethyl aluminum chloride, or boron trifluoride to a reaction zone maintained at a temperature in the range of about -120° C. to about -20° C. to form a reaction mixture; (b) maintaining said reaction mixture in said reaction zone at said temperature for a time sufficient to convert at least one of said monomers to said interpolymer in an amount equal to or greater than about 85 percent; and (c) recovering said interpolymer from the effluent reaction mixture leaving said reaction zone.
Claim 3
Dependent Claim
188 words
A continuous process for the preparation of gel-free interpolymers comprised of a. about 0.5 to 5.0 mole percent of a mixture of 3-chloromethyl styrene and 4-chloromethyl styrene and b. one or more monoolefins represented by the formula R'(R")C = CH 2 wherein R' and R" are independently selected from the group consisting of C 1 to C 15 alkyl, aryl, alkylaryl, arylalkyl and cycloalkyl radicals, which comprises: (A) continuously feeding to a reaction zone the monomers, solvent system and a soluble catalyst selected from the group consisting of ethyl aluminum dichloride, ethyl aluminum sesquichloride and diethyl aluminum chloride, said catalyst being fed to said reaction zone in a concentration in the range of 0.001 to 0.05 weight percent of the total of the monomers and solvents at the said reaction zone. (B) maintaining the reaction mixture in the reaction zone at a temperature from -120° C. to -20° C. for a time sufficient to convert at least one of the monomers to the interpolymer in an amount equal to or greater than 85 percent; and (C) recovering the interpolymer from the effluent reaction mixture leaving the reaction zone.
Claim 4
Dependent Claim
188 words
A continuous process for the preparation of gel-free interpolymers comprised of a. about 0.5 to 5.0 mole percent of a mixture of 3-chloromethyl styrene and 4-chloromethyl styrene and b. one or more monoolefins represented by the formula R'(R")C = CH 2 wherein R' and R" are independently selected from the group consisting of C 1 to C 15 alkyl, aryl, alkylaryl, arylalkyl and cycloalkyl radicals, which comprises: (A) continuously feeding to a reaction zone the monomers, solvent system and a soluble catalyst selected from the group consisting of ethyl aluminum dichloride, ethyl aluminum sesquichloride and diethyl aluminum chloride, said catalyst being fed to said reaction zone in a concentration in the range of 0.001 to 0.05 weight percent of the total of the monomers and solvents at the said reaction zone. (B) maintaining the reaction mixture in the reaction zone at a temperature from -120° C. to -20° C. for a time sufficient to convert at least one of the monomers to the interpolymer in an amount equal to or greater than 85 percent; and (C) recovering the interpolymer from the effluent reaction mixture leaving the reaction zone.
References Cited (Backward Citations)
US2974126A
Cited
US3067182A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-02-13 | 1981-08-15 | 1982-02-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-02-13 | 1985-08-15 | 1986-02-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-02-13 | 1989-08-15 | 1990-02-14 | $7700.00 | Window Closed / Lapsed |