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US3816379A Expired / Lapsed US ⏱️ 0.0 years remaining

Monomer and solvent recovery in polymerization processes

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1971-07-26
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Granted: 1974-06-11
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Expires: 1991-07-26
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Abstract

Abstract Improvements in the process for preparing copolymers of ethylene, higher alpha-olefins and, optionally as termonomer, a nonconjugated diene include subjecting the reactor effluent containing polymer cement, unreacted monomers, catalyst composition, and diluent-solvent to a first stripping operation, wherein recycled vaporous diluent-solvent is used as stripping medium, whereby substantially all unreacted light monomers and some diluent-solvent are taken as overhead. The first stripper bottoms are deashed and subjected to a second stripping operation employing steam as stripping medium. The overhead of this second operation, containing substantially all remaining diluent-solvent and some steam, is condensed; most water is withdrawn therefrom and the remaining water-saturated diluent-solvent is fractionated separating as overhead, any remaining water and any light impurities, and, as bottoms dry diluent-solvent and any heavy impurities. These bottoms are again fractionated separating as overhead, pure hot vaporous diluent-solvent which is recycled to the first stripping operation as stripping medium, and, as bottoms heavy impurities and any heavy termonomer. The overhead of the first stripping operation may be partially condensed, separating as overhead light monomers, any light impurities, and some diluent-solvent. The condensate containing a major portion of diluent-solvent and minor amounts of light monomer may be directly recycled to the reactor. The noncondensed portion may be fractionated, thereby separating substantially all unreacted light monomer as overhead which may be recycled directly to the reactor. The bottoms, containing diluent-solvent and light impurities, may be combined with the overhead from the second stripping operation. This process results in improved and simplified monomer and diluent-solvent recycle and significant investment and operating cost savings due to improved heat integration and reduction of required processing equipment.

Inventors

  • 👤 J Faure
  • 👤 J Love
  • 👤 H Rosenbaum
  • 👤 B Tegge

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 16:45
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/06

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 69 words
The process of claim 1 wherein said first stripping operation is performed at a temperature in the range of about 65* to about 95*C. and at a pressure at least about 2 atm. below reactor pressure, and said second stripping operation is performed at a temperature in the range of about 65* to about 115*C. and at a pressure in the range of about 1 to about 3 atm.
Claim 2
Dependent Claim 8 words
recycling said condensate of diluent-solvent to said reactor;
Claim 3
Dependent Claim 19 words
fractionating said noncondensed portion thereby separating as overhead substantially all unreacted monomers and, as bottoms, light impurities and diluent-solvent;
Claim 4
Dependent Claim 65 words
The process of claim 1 wherein the fractionation of step (D) is performed at a temperature in the range of about 65* to about 175*C. and a pressure in the range of about 1.5 to about 8 atm. and the fractionation of step (E) is performed at a temperature of about 80* to about 175*C. and a pressure of about 1.5 to about 8 atm.
Claim 5
Dependent Claim 10 words
The process of claim 1 wherein said diluent-solvent is hexane.
Claim 6
Dependent Claim 13 words
recycling said overhead of step (3) containing unreacted monomers to said reactor, and
Claim 7
Dependent Claim 17 words
combining said bottoms from step (3) with the overhead from the second stripper operation of claim 1.
Claim 8
Dependent Claim 11 words
The process of claim 1 which further comprises the steps of:
Claim 9
Dependent Claim 71 words
The process of claim 5 wherein the partial condensation of step (1) is performed at a temperature in the range of about 10* to about 65*C. and a pressure of about 1 to about 1.5 atm., and the fractionation of step (3) is performed at a temperature in the range of from about -15* to about 150*C. and a pressure in the range of from about 2.5 to about 11 atm.
Claim 10
Dependent Claim 32 words
The process of claim 5 wherein said reactants additionally include a nonconjugated diene and the copolymer formed is a terpolymer of ethylene, a C3 to C10 higher alpha-olefin, and a nonconjugated diene.
Claim 11
Dependent Claim 10 words
The process of claim 7 wherein said alpha-olefin is propylene.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-06-10 1977-12-10 1978-06-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-06-10 1981-12-10 1982-06-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-06-10 1985-12-10 1986-06-11 $7700.00 Window Closed / Lapsed

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