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Continuous process for production of copolymer of an alkali metal vinyl sulfonate and acrylic acid

Assignee: ChampionX LLC
•
Filing: 1980-05-27
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Granted: 1982-05-25
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Expires: 2000-05-27
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Abstract

Abstract There is provided a continuous process for the production of a copolymer of an alkali metal vinyl sulfonate and acrylic acid. The process comprises continuously feeding an aqueous solution of an alkali metal vinyl sulfonate and acrylic acid together with a polymerization initiator to a reaction zone. The reaction zone is operated adiabatically at a temperature sufficiently high to affect copolymerization of the alkali metal vinyl sulfonate and acrylic acid. The alkali metal vinyl sulfonate and acrylic acid are maintained in the reaction zone for a residence time sufficient to form a copolymer of these two monomers. The resultant copolymer is continuously removed from the reaction zone.

Inventors

  • 👤 Louis A. Goretta
  • 👤 Robert R. Otremba

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 08:29
CPC Classifications
C; C08; C08F; C08F228/00; C08F228/02; C08F220/00; C08F220/02; C08F220/04; C08F220/06

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 115 words
A continuous process for the production of a copolymer of an alkali metal vinyl sulfonate and acrylic acid which comprises continuously feeding an aqueous solution of an alkali metal vinyl sulfonate and acrylic acid together with a polymerization initiator to a reaction zone and copolymerizing said alkali metal vinyl sulfonate and acrylic acid, said reaction zone being maintained at a temperature sufficiently high to effect copolymerization of said alkali metal vinyl sulfonate and acrylic acid, the residence time of said alkali metal vinyl sulfonate and acrylic acid in said reaction zone being sufficient to form a copolymer thereof and being from about three to ten minutes, and continuously recovering said copolymer from said reaction zone.
Claim 2
Dependent Claim 115 words
A continuous process for the production of a copolymer of an alkali metal vinyl sulfonate and acrylic acid which comprises continuously feeding an aqueous solution of an alkali metal vinyl sulfonate and acrylic acid together with a polymerization initiator to a reaction zone and copolymerizing said alkali metal vinyl sulfonate and acrylic acid, said reaction zone being maintained at a temperature sufficiently high to effect copolymerization of said alkali metal vinyl sulfonate and acrylic acid, the residence time of said alkali metal vinyl sulfonate and acrylic acid in said reaction zone being sufficient to form a copolymer thereof and being from about three to ten minutes, and continuously recovering said copolymer from said reaction zone.
Claim 3
Dependent Claim 17 words
A process as defined in claim 1 wherein said alkali metal vinyl sulfonate is sodium vinyl sulfonate.
Claim 4
Dependent Claim 27 words
A process as defined in claim 2 wherein said sodium vinyl sulfonate and acrylic acid are mixed together with water before being fed to said reaction zone.
Claim 5
Dependent Claim 39 words
A process as defined in claim 3 wherein the pH of said solution of sodium vinyl sulfonate and acrylic acid is adjusted to within the range of from about 4.0 to 5.5 before being fed to said reaction zone.
Claim 6
Dependent Claim 15 words
A process as defined in claim 3 wherein said polymerization initiator is a redox catalyst.
Claim 7
Dependent Claim 17 words
A process as defined in claim 5 wherein said redox catalyst comprises ammonium persulfate and sodium bisulfite.
Claim 8
Dependent Claim 30 words
A process as defined in claim 6 wherein an aqueous solution of said ammonium persulfate and an aqueous solution of said sodium bisulfite are separately fed to said reaction zone.
Claim 9
Dependent Claim 27 words
A process as defined in claim 3 wherein said reaction zone is operated adiabatically at a temperature of from about 120° to 250° F. during said process.
Claim 10
Dependent Claim 27 words
A process as defined in claim 3 wherein said reaction zone is operated adiabatically at a temperature of from about 140° to 220° F. during said process.
Claim 11
Dependent Claim 30 words
A process as defined in claim 3 wherein the residence time of said sodium vinyl sulfonate and acrylic acid in said reaction zone is from about 5 to 7 minutes.
Claim 12
Dependent Claim 25 words
A process as defined in claim 3 wherein from about 0.01 to 0.5 mole of sodium vinyl sulfonate per mole of acrylic acid is employed.
Claim 13
Dependent Claim 25 words
A process as defined in claim 3 wherein from about 0.05 to 0.25 mole of sodium vinyl sulfonate per mole of acrylic acid is employed.

References Cited (Backward Citations)

US3755236A Cited
US4076928A Cited
US4164489A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-05-24 1985-11-23 1986-05-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-05-24 1989-11-23 1990-05-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-05-24 1993-11-23 1994-05-25 $7700.00 Window Closed / Lapsed

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