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US3983096A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymerization process under pressure in an annular equipment

Assignee: Montedison SpA
•
Filing: 1974-10-15
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Granted: 1976-09-28
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Expires: 1994-10-15
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Abstract

Abstract An annular reactor for polymerizing and copolymerizing vinyl esters characterized by the fact that the height to width ratio is greater than 1 and preferably greater than 5, that there is a circulating pump in the lower leg of the reactor and that the pump delivery volume of the reactor is between 5 and 30 percent of the reactor total volume, and preferably about 15 percent of the reactor total volume. Methods of polymerizing and copolymerizing vinyl monomers in such a reactor are also disclosed.

Inventors

  • 👤 Angelo Segalini

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 18:09
CPC Classifications
B; B01; B01J; B01J19/00; B01J19/18; B01J19/1812; B01J19/1837; B01J3/00; B01J3/04; B01J3/042; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00087; B01J2219/00094

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 85 words
In a process for polymerizing under pressure fluid vinyl monomers which are gradually admixed to an initial reaction medium containing a portion of monomer, wherein the improvement comprises conducting the polymerization in an annular reactor including bottom and top legs joined by two vertical legs and having a height to width ratio greater than 1, a circulating pump in said bottom leg, the vertical leg into which said pump discharges having a volume of between about 5 and 30 percent of the reactor total volume.
Claim 2
Dependent Claim 85 words
In a process for polymerizing under pressure fluid vinyl monomers which are gradually admixed to an initial reaction medium containing a portion of monomer, wherein the improvement comprises conducting the polymerization in an annular reactor including bottom and top legs joined by two vertical legs and having a height to width ratio greater than 1, a circulating pump in said bottom leg, the vertical leg into which said pump discharges having a volume of between about 5 and 30 percent of the reactor total volume.
Claim 3
Dependent Claim 14 words
Polymerization process of claim 1, wherein the monomers are polymerized in an aqueous emulsion.
Claim 4
Dependent Claim 10 words
Polymerization process of claim 1, wherein vinyl acetate is polymerized.
Claim 5
Dependent Claim 18 words
Polymerization process of claim 1, wherein a mixture of vinyl esters and gaseous ethylenically unsaturated monomers is polymerized.
Claim 6
Dependent Claim 24 words
Polymerization process of claim 4, wherein vinyl acetate ethylene copolymers having an ethylene content ranging from 5 to 50 percent by weight as prepared.
Claim 7
Dependent Claim 38 words
Polymerization process of claim 4, wherein vinyl acetate ethylene-vinyl chloride terpolymers having an ethylene content of between 5 and 40 percent by weight and a vinyl chloride content of between 5 and 40 percent by weight are prepared.

References Cited (Backward Citations)

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US3324093A Cited
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US3668165A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-09-28 1980-03-29 1980-09-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-09-28 1984-03-29 1984-09-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-09-28 1988-03-29 1988-09-28 $7700.00 Window Closed / Lapsed

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