← Back to Patent Explorer
US4117216A Expired / Lapsed US ⏱️ 0.0 years remaining

Inversion polymerization process for producing vinyl resins

Assignee: Geon Co
•
Filing: 1977-09-02
•
Granted: 1978-09-26
•
Expires: 1997-09-02
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract This invention relates to a process of producing vinyl polymers by an inversion polymerization technique in the presence of a coating on the internal surfaces of the polymerization reactor. By inversion polymerization is meant conducting the initial stage of the polymerization reaction wherein the monomer or monomers being polymerized constitute the continuous phase and in the latter stage of polymerization, water constitutes the continuous phase. The coating is comprised of a water-soluble suspending agent, such as an alkyl or alkyl hydroxyalkyl cellulose ether. By means of the present inventive process, polymer buildup on the internal surfaces of the reactor are reduced.

Inventors

  • 👤 Donald Edward Witenhafer
  • 👤 David Thomas Popovich

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 07:38
CPC Classifications
C; C08; C08F; C08F2/00; C08F2/02; C08F2/002; C08F2/004

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 195 words
In a process of inversion polymerizing substantially water-insoluble polymerizable ethylenically unsaturated monomer(s) in a reaction vessel by first forming a continuous monomer(s) phase in the presence of a monomer-soluble surface active agent and a monomer-soluble catalyst, polymerizing said monomer phase at a temperature in the range of about 30° C. to about 80° C. with agitation until a conversion to polymer less than about 20% occurs, adding sufficient water to the monomer-polymer mixture with agitation and in the presence of at least about 0.1% by weight of a water-soluble suspending agent for said monomer(s) to form a dispersion wherein water is the continuous phase, then polymerizing the dispersion at a temperature in the range of about 30° C. to about 80° C. to convert the remaining monomer(s) to polymer, the improvement which comprises (1) applying a coating to the internal surfaces of said reaction vessel, comprised of a water-soluble suspending agent, (2) polymerizing the continuous monomer phase in constant contact with said coating, and (3) polymerizing said continuous water phase in constant contact with said coating while dissolving said coating in the continuous water phase, whereby polymer buildup on said internal surfaces is substantially reduced.
Claim 2
Dependent Claim 195 words
In a process of inversion polymerizing substantially water-insoluble polymerizable ethylenically unsaturated monomer(s) in a reaction vessel by first forming a continuous monomer(s) phase in the presence of a monomer-soluble surface active agent and a monomer-soluble catalyst, polymerizing said monomer phase at a temperature in the range of about 30° C. to about 80° C. with agitation until a conversion to polymer less than about 20% occurs, adding sufficient water to the monomer-polymer mixture with agitation and in the presence of at least about 0.1% by weight of a water-soluble suspending agent for said monomer(s) to form a dispersion wherein water is the continuous phase, then polymerizing the dispersion at a temperature in the range of about 30° C. to about 80° C. to convert the remaining monomer(s) to polymer, the improvement which comprises (1) applying a coating to the internal surfaces of said reaction vessel, comprised of a water-soluble suspending agent, (2) polymerizing the continuous monomer phase in constant contact with said coating, and (3) polymerizing said continuous water phase in constant contact with said coating while dissolving said coating in the continuous water phase, whereby polymer buildup on said internal surfaces is substantially reduced.
Claim 3
Dependent Claim 16 words
A process as defined in claim 1 wherein the coating is an alkyl hydroxyalkyl cellulose ether.
Claim 4
Dependent Claim 16 words
A process as defined in claim 1 wherein the continuous monomer phase is a water-in-monomer dispersion.
Claim 5
Dependent Claim 13 words
A process as defined in claim 1 wherein the monomer is vinyl chloride.
Claim 6
Dependent Claim 44 words
A process as defined in claim 1 wherein the monomer-soluble surface active agent is selected from the group consisting of nonionic esters of fatty acids with glycerol, sorbitol and their polyoxyethylene derivatives and nonionic multi-valent metal salts of fatty acids, alkyl sulfonates and sulfates.
Claim 7
Dependent Claim 14 words
A process as defined in claim 1 wherein the coating is hydroxypropyl methyl cellulose.
Claim 8
Dependent Claim 15 words
A process as defined in claim 5 wherein the surface active agent is sorbitan monostearate.
Claim 9
Dependent Claim 14 words
A process as defined in claim 2 wherein the coating is hydroxypropyl methyl cellulose.

References Cited (Backward Citations)

US3515709A Cited
US3669946A Cited
US3778423A Cited
US3804924A Cited
US3915944A Cited
US4007320A Cited
US4024301A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-09-25 1982-03-27 1982-09-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-09-25 1986-03-27 1986-09-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-09-25 1990-03-27 1990-09-26 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag