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US4623712A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for high temperature phase separation of solutions containing polymers

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1984-06-25
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Granted: 1986-11-18
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Expires: 2004-06-25
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Abstract

Abstract A process is disclosed for recovering polymer from a solution of the polymer in a solvent by high temperature phase separation in which low molecular weight hydrocarbon is added to the solution, the solution and the added hydrocarbon are subjected to a temperature and pressure so that one liquid phase is formed and the pressure is adjusted to form two phases, namely, a polymer-lean liquid phase and a polymer-rich liquid phase. The polymer-rich liquid phase is separated from the polymer-lean liquid phase, and the polymer is then recovered from the polymer-rich liquid phase.

Inventors

  • 👤 Cyrus A. Irani
  • 👤 Charles Cozewith
  • 👤 Stephen S. Kasegrande

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 17:59
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/06; C08F6/12

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 251 words
A process for the recovery of hydrocarbon polymer from a solution of said polymer comprising: (i) preparing the solution of polymer in a reactor; (ii) adding to the thus-prepared solution of polymer an effective amount of at least one low molecular weight hydrocarbon selected from the group consisting of unsubstituted and halogenated C 1 alkanes and halogenated C 2 -C 4 alkanes, alkenes, alkynes with the proviso that said hydrocarbon is a gas at ambient temperature and pressure; provided, however, that where the low molecular weight hydrocarbon is a C 1 halogenated or unhalogenated alkane, it is utilized at about 2 to about 10.8 wt. % based on the polymer solution, and further provided that where the low molecular weight hydrocarbon is a C 2 halogenated or unhalogenated alkane, alkene, or alkyne, it is utilized at about 2 to about 21 wt. % based on the polymer solution; still further provided that where the low molecular weight hydrocarbon is a C 3 -C 4 halogenated or unhalogenated hydrocarbon it is utilized at about 2 to about 30 wt. % based on the polymer solution; (iii) subjecting said solution including said hydrocarbon to a temperature at which two liquid phases can form and a pressure sufficient to prevent the creation of a vapor phase; (iv) adjusting said pressure such that a polymer-rich liquid phase and a polymer-lean liquid phase are formed; (v) separating said polymer-rich liquid phase from said polymer-lean liquid phase; and (vi) recovering said polymer from said polymer-rich liquid phase.
Claim 2
Dependent Claim 251 words
A process for the recovery of hydrocarbon polymer from a solution of said polymer comprising: (i) preparing the solution of polymer in a reactor; (ii) adding to the thus-prepared solution of polymer an effective amount of at least one low molecular weight hydrocarbon selected from the group consisting of unsubstituted and halogenated C 1 alkanes and halogenated C 2 -C 4 alkanes, alkenes, alkynes with the proviso that said hydrocarbon is a gas at ambient temperature and pressure; provided, however, that where the low molecular weight hydrocarbon is a C 1 halogenated or unhalogenated alkane, it is utilized at about 2 to about 10.8 wt. % based on the polymer solution, and further provided that where the low molecular weight hydrocarbon is a C 2 halogenated or unhalogenated alkane, alkene, or alkyne, it is utilized at about 2 to about 21 wt. % based on the polymer solution; still further provided that where the low molecular weight hydrocarbon is a C 3 -C 4 halogenated or unhalogenated hydrocarbon it is utilized at about 2 to about 30 wt. % based on the polymer solution; (iii) subjecting said solution including said hydrocarbon to a temperature at which two liquid phases can form and a pressure sufficient to prevent the creation of a vapor phase; (iv) adjusting said pressure such that a polymer-rich liquid phase and a polymer-lean liquid phase are formed; (v) separating said polymer-rich liquid phase from said polymer-lean liquid phase; and (vi) recovering said polymer from said polymer-rich liquid phase.
Claim 3
Dependent Claim 33 words
A process according to claim 1 wherein from about 2 to about 30 weight % of a C 3 -C 4 hydrocarbon based on the polymer solution, is added to said polymer solution.
Claim 4
Dependent Claim 13 words
A process according to claim 2, wherein said polymer comprises ethylene-propylene copolymer elastomer.
Claim 5
Dependent Claim 21 words
A process according to claim 2, wherein said polymer comprises a terpolymer of ethylene, a higher alpha-olefin and a non-conjugated diene.
Claim 6
Dependent Claim 18 words
A process according to claim 4, wherein said polymer is a terpolymer of ethylene, propylene and 5-ethylidene norbornene.
Claim 7
Dependent Claim 12 words
A process according to claim 2, wherein said polymer comprises halobutyl rubber.
Claim 8
Dependent Claim 13 words
A process according to claim 6, wherein said halobutyl rubber comprises chlorobutyl rubber.
Claim 9
Dependent Claim 23 words
A process according to claim 1, wherein said solvent is a member selected from the group consisting of aliphatic, aromatic and halogenated hydrocarbons.
Claim 10
Dependent Claim 18 words
A process according to claim 1, wherein said solvent is a C 5 to C 7 aliphatic hydrocarbon.
Claim 11
Dependent Claim 36 words
A process according to claim 1, wherein said solution of polymer prepared in a reactor exits from said reactor as an effluent stream, and wherein said low molecular weight hydrocarbon is added to said effluent stream.
Claim 12
Dependent Claim 43 words
A process according to claim 1, wherein after preparation of said solution of polymer in said reactor, reaction mixture from said reactor is deashed to remove catalyst residues, and wherein said low molecular weight hydrocarbon is added to said reaction mixture after deashing.
Claim 13
Dependent Claim 32 words
A process according to claim 1, wherein said low molecular weight hydrocarbon is selected from the group consisting of unsubstituted C 1 alkane and unsubstituted C 2 -C 4 alkanes and alkenes.
Claim 14
Dependent Claim 17 words
A process according to claim 1, wherein said low molecular weight hydrocarbon is unsubstituted C 1 alkane.
Claim 15
Dependent Claim 20 words
A process according to claim 1, wherein said low molecular weight hydrocarbon is at least one halogenated C 1 alkane.
Claim 16
Dependent Claim 22 words
A process according to claim 1, wherein said low molecular weight hydrocarbon is at least one halogenated C 2 -C 4 alkane.
Claim 17
Dependent Claim 22 words
A process according to claim 1, wherein said low molecular weight hydrocarbon is at least one halogenated C 2 -C 4 alkene.
Claim 18
Dependent Claim 22 words
A process according to claim 1, wherein said low molecular weight hydrocarbon is at least one halogenated C 2 -C 4 alkyne.
Claim 19
Dependent Claim 20 words
A process according to claim 1, wherein in step (iv) a vapor phase rich in said hydrocarbon is also formed.

References Cited (Backward Citations)

US4319021A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-11-17 1990-05-19 1990-11-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-11-17 1994-05-19 1994-11-18 $3760.00 Window Closed / Lapsed
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