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US4292424A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for recovering vinyl polymers from emulsion polymerization latices

Assignee: Geon Co
•
Filing: 1980-03-03
•
Granted: 1981-09-29
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Expires: 2000-03-03
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Abstract

Abstract The invention relates to the production of vinyl dispersion or paste resins by means of the emulsion polymerization process and the recovery of the resins from the polymer latices produced thereby. In the process, the polymer latex is first carefully coagulated to yield a fast filtering sludge, the sludge is passed to a pressure filter to separate a high solids, friable polymer wetcake from the serum, the wetcake is rinsed with proper agents to neutralize the same and remove undesirable residues, pressure in the filter is applied to the rinsed wetcake to increase the solids content thereof, the wetcake is then broken into particles and friable agglomerates, and thereafter said particles and agglomerates are dried and ground to proper size in one step in a fluid energy mill. Thus the spray drying and the subsequent harsh grinding steps are eliminated producing a superior product for plastisols.

Inventors

  • 👤 George R. Huddleston, Jr.
  • 👤 James W. Turner
  • 👤 Kenneth D. Konter

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 18:10
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/14; C08F14/00; C08F14/02; C08F14/04; C08F14/06

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 284 words
A process for producing polymers of vinyl and vinylidene halides and copolymers thereof with each other or either with one or more polymerizable unsaturated olefinic monomers which comprises forming a monomer premix containing an aqueous reaction medium, the monomer or monomers to be polymerized, a free radical yielding catalyst, and at least one emulsifier, homogenizing said premix and passing the same to a reaction zone, polymerizing said premix in said zone at a temperature in the range of about 30° C. to about 70° C. and at a pH of about 3 to about 12 to produce a vinyl polymer latex, passing said latex through a stripping zone to remove unreacted monomer(s) therefrom with steam, passing said stripped latex to a coagulation zone, adding a coagulating agent to said latex in said coagulation zone at a pH in the range of about 2 to about 8 to form a slurry of friable agglomerates of polymer particles in a serum, passing said slurry to a pressure filter zone wherein the serum is removed under pressure through a permeable membrane and a wetcake of polymer is formed, rinsing said wetcake to remove residual compounds therefrom, pressing said wetcake to a solids content in the range of about 65% to about 75% by weight, passing said wetcake to a crumbling zone and breaking the same to form friable polymer agglomerates and particles, passing said polymer agglomerates and particles into a fluid energy mill while injecting heated air into said mill under a pressure in the range of about 2.5 psig. to about 80 psig. thereby grinding and drying said polymer agglomerates and particles, and recovering the polymer from said mill in the form of discrete particles thereof.
Claim 2
Dependent Claim 284 words
A process for producing polymers of vinyl and vinylidene halides and copolymers thereof with each other or either with one or more polymerizable unsaturated olefinic monomers which comprises forming a monomer premix containing an aqueous reaction medium, the monomer or monomers to be polymerized, a free radical yielding catalyst, and at least one emulsifier, homogenizing said premix and passing the same to a reaction zone, polymerizing said premix in said zone at a temperature in the range of about 30° C. to about 70° C. and at a pH of about 3 to about 12 to produce a vinyl polymer latex, passing said latex through a stripping zone to remove unreacted monomer(s) therefrom with steam, passing said stripped latex to a coagulation zone, adding a coagulating agent to said latex in said coagulation zone at a pH in the range of about 2 to about 8 to form a slurry of friable agglomerates of polymer particles in a serum, passing said slurry to a pressure filter zone wherein the serum is removed under pressure through a permeable membrane and a wetcake of polymer is formed, rinsing said wetcake to remove residual compounds therefrom, pressing said wetcake to a solids content in the range of about 65% to about 75% by weight, passing said wetcake to a crumbling zone and breaking the same to form friable polymer agglomerates and particles, passing said polymer agglomerates and particles into a fluid energy mill while injecting heated air into said mill under a pressure in the range of about 2.5 psig. to about 80 psig. thereby grinding and drying said polymer agglomerates and particles, and recovering the polymer from said mill in the form of discrete particles thereof.
Claim 3
Dependent Claim 13 words
The process as defined in claim 1 wherein the monomer is vinyl chloride.
Claim 4
Dependent Claim 28 words
The process as defined in claim 1 wherein the total solids content of the stripped latex is in the range of about 5% to about 50% by weight.
Claim 5
Dependent Claim 33 words
A process as defined in claim 1 where the amount of coagulating agent is in the range of about 0 ppm. to about 50,000 ppm. based on the amount of resin being treated.
Claim 6
Dependent Claim 30 words
A process as defined in claim 1 wherein the temperature of the air in the fluid energy mill is in the range of about 50° C. to about 80° C.
Claim 7
Dependent Claim 14 words
A process as defined in claim 1 wherein the coagulating agent is calcium chloride.
Claim 8
Dependent Claim 14 words
The process as defined in claim 1 wherein the coagulating agent is aluminum sulfate.
Claim 9
Dependent Claim 16 words
The process as defined in claim 1 wherein the coagulating agent is a polymeric modified polyamine.
Claim 10
Dependent Claim 23 words
A process as defined in claim 1 wherein the rinsing is done with an aqueous solution of ammonium hydroxide or alkali metal hydroxide.
Claim 11
Dependent Claim 15 words
A process as defined in claim 1 wherein the rinsing solution contains a chelating agent.
Claim 12
Dependent Claim 25 words
A process as defined in claim 1 wherein the chelating agent is selected from the sodium salts and ammonium salts of ethylene diamine tetra-acetic acid.
Claim 13
Dependent Claim 34 words
A process as defined in claim 3 wherein the amount of the coagulating agent is in the range of about 0 ppm. to about 50,000 ppm. based on the amount of resin being treated.
Claim 14
Dependent Claim 14 words
A process as defined in claim 12 wherein the coagulating agent is aluminum sulfate.
Claim 15
Dependent Claim 19 words
A process as defined in claim 13 wherein the rinsing is done with an aqueous solution of ammonium hydroxide.
Claim 16
Dependent Claim 15 words
A process as defined in claim 14 wherein the rinsing solution contains a chelating agent.
Claim 17
Dependent Claim 29 words
A process as defined in claim 15 wherein the temperature of the air in the drying zone is in the range of about 50° C. to about 80° C.
Claim 18
Dependent Claim 20 words
A process as defined in claim 15 wherein the chelating agent is the sodium salt of ethylene diamine tetra-acetic acid.
Claim 19
Dependent Claim 21 words
A process as defined in claim 13 wherein the rinsing is done with an aqueous solution of an alkali metal hydroxide.

References Cited (Backward Citations)

US2844568A Cited
US3595840A Cited
US3901842A Cited
US3954910A Cited
US3956249A Cited
US4197399A Cited
US4138539A Cited
US4168373A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-09-28 1985-03-30 1985-09-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-09-28 1989-03-30 1989-09-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-09-28 1993-03-30 1993-09-29 $7700.00 Window Closed / Lapsed

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