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US3954910A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for removal and recovery of unreacted monomers from resinous polymers

Assignee: Standard Oil Co
•
Filing: 1974-04-12
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Granted: 1976-05-04
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Expires: 1994-04-12
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Abstract

Abstract The invention is concerned with the effecient removal and recovery of unreacted monomers from polymer latices prepared by emulsion polymerization.

Inventors

  • 👤 Einar Peter Kropp
  • 👤 John Wesley Hougland
  • 👤 Gary Grant Innocenti

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 18:39
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/14; C08F6/16

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 170 words
In the process for producing a monomerfree resinous polymer wherein said polymer is prepared by the emulsion polymerization of a major portion of a monounsaturated nitrile and optionally another monovinyl monomer copolymerizable therewith, in an aqueous medium and optionally in the presence of a preformed diene rubber which may be a homopolymer or a copolymer of a conjugated diene monomer, and wherein the polymeric latex prepared in said polymerization reaction is coagulated, the resulting coagulum is hardened and washed with water, and the essentially monomer-free resinous polymer recovered therefrom, the improvement comprising: removing and recovering unreacted monomer from the coagulated latex of said polymer during the hardening and washing steps of the process by: A. heating a slurry of the monomer-containing coagulum of said polymer in an aqueous bath maintained at a temperature in the range of from about 10°C above to 10°C below the heat distortion temperature of the polymer, to set the polymer and to remove some of the monomer therefrom; B. partially dewatering the coagulum from (A);
Claim 2
Dependent Claim 170 words
In the process for producing a monomerfree resinous polymer wherein said polymer is prepared by the emulsion polymerization of a major portion of a monounsaturated nitrile and optionally another monovinyl monomer copolymerizable therewith, in an aqueous medium and optionally in the presence of a preformed diene rubber which may be a homopolymer or a copolymer of a conjugated diene monomer, and wherein the polymeric latex prepared in said polymerization reaction is coagulated, the resulting coagulum is hardened and washed with water, and the essentially monomer-free resinous polymer recovered therefrom, the improvement comprising: removing and recovering unreacted monomer from the coagulated latex of said polymer during the hardening and washing steps of the process by: A. heating a slurry of the monomer-containing coagulum of said polymer in an aqueous bath maintained at a temperature in the range of from about 10°C above to 10°C below the heat distortion temperature of the polymer, to set the polymer and to remove some of the monomer therefrom; B. partially dewatering the coagulum from (A);
Claim 3
Dependent Claim 98 words
C. washing the partially dewatered coagulum from (B) in an aqueous bath maintained at a temperature within the range of from about 20°C below and up to the heat distortion temperature of the polymer; D. dewatering and removing any remaining monomer from the coagulum in (C) and drying and recovering the essentially monomer-free polymer therefrom; E. scrubbing the monomer from the vapors derived from steps (A) through (D) in an aqueous absorption zone; F. stripping overhead the monomer from the monomer-rich aqueous effluents from steps (B) and (E) and decanting the overhead to recover essentially pure monomer therefrom.
Claim 4
Dependent Claim 98 words
C. washing the partially dewatered coagulum from (B) in an aqueous bath maintained at a temperature within the range of from about 20°C below and up to the heat distortion temperature of the polymer; D. dewatering and removing any remaining monomer from the coagulum in (C) and drying and recovering the essentially monomer-free polymer therefrom; E. scrubbing the monomer from the vapors derived from steps (A) through (D) in an aqueous absorption zone; F. stripping overhead the monomer from the monomer-rich aqueous effluents from steps (B) and (E) and decanting the overhead to recover essentially pure monomer therefrom.
Claim 5
Dependent Claim 19 words
The process in claim 1 wherein the coagulum in (A) is obtained by paste coagulation of the polymeric latex.
Claim 6
Dependent Claim 25 words
The process in claim 1 wherein the coagulum in (A) is obtained by crumb coagulation of the polymeric latex in the aqueous bath of A.
Claim 7
Dependent Claim 22 words
The process in claim 2 wherein some of the essentially monomer-free effluent from step (F) is recycled for use in step (E).
Claim 8
Dependent Claim 21 words
The process in claim 1 wherein the mono-unsaturated nitrile is a member selected from the group consisting of acrylonitrile and methacrylonitrile.
Claim 9
Dependent Claim 27 words
The process in claim 1 wherein the monovinyl monomer is a member selected from the group consisting of methyl acrylate, ethyl acrylate, methyl methacrylate, and ethyl methacrylate.
Claim 10
Dependent Claim 18 words
The process in claim 1 wherein the water recovered from (D) is recycled to the bath in (A).
Claim 11
Dependent Claim 11 words
The process in claim 5 wherein the monovinyl monomer is styrene.

References Cited (Backward Citations)

US3006872A Cited
US3345430A Cited
US3248455A Cited
US3821348A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-05-04 1979-11-03 1980-05-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-05-04 1983-11-03 1984-05-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-05-04 1987-11-03 1988-05-04 $7700.00 Window Closed / Lapsed

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