Patent US4994931A successfully refreshed from Google Patents.
← Back to Patent Explorer
US4058652A Expired / Lapsed US ⏱️ 0.0 years remaining

Autorefrigeration process and apparatus

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1976-02-10
•
Granted: 1977-11-15
•
Expires: 1996-02-10
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract The fouling of autorefrigeration polymerization systems because of entrained particles in the vaporized solvent-diluent is substantially reduced by returning the recycle solvent-diluent into the reaction zone through nozzles which provide a solvent-diluent spray of an average droplet size of less than 1000 microns, preferably between about 225 and 300 micron average particle size, which spray removes major amounts of entrained particles down to 5 microns in size. The solvent diluent may be an inert material or unreacted alpha-olefin, such as propylene.

Inventors

  • 👤 Stuart B. Smith
  • 👤 James J. McAlpin
  • 👤 Jose M. A. Peruyero
  • 👤 Ronald L. Hazelton
  • 👤 Edward F. Upchurch

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 22:27
CPC Classifications
C; C23; C23F; C23F15/00; C23F15/005; B; B01; B01J; B01J19/00; B01J19/0006; B01J19/0013; B01J19/18; C08; C08F; C08F10/00; C08F2/00; C08F2/04; C08F2/06; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00105; B01J2219/00108; B01J2219/00121; B01J2219/0013; B01J2219/18; B01J2219/185

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 140 words
In an autorefrigeration reaction of alpha-olefins to produce polymers comprising reacting C 2 to C 8 alpha-olefins in the presence of a catalyst at temperatures in the range of 20° to 80° C in a solvent-diluent in liquid phase in a reaction zone, vaporizing a portion of said solvent-diluent from the liquid phase in said reaction zone, said vaporized solvent-diluent containing entrained polymer particles in the range of 3 to 15 microns, removing, condensing said solvent-diluent, and returning a portion of said solvent-diluent to said reaction zone, wherein the improvement comprises returning condensed, solvent-diluent to said reaction zone as a spray, having a drop average particle size of less than 1000 microns, said vaporized solvent-diluent passing through said spray whereby over 50 weight % of said entrained polymer particles of 5 microns and larger are removed from said vaporized solvent-diluent.
Claim 2
Dependent Claim 140 words
In an autorefrigeration reaction of alpha-olefins to produce polymers comprising reacting C 2 to C 8 alpha-olefins in the presence of a catalyst at temperatures in the range of 20° to 80° C in a solvent-diluent in liquid phase in a reaction zone, vaporizing a portion of said solvent-diluent from the liquid phase in said reaction zone, said vaporized solvent-diluent containing entrained polymer particles in the range of 3 to 15 microns, removing, condensing said solvent-diluent, and returning a portion of said solvent-diluent to said reaction zone, wherein the improvement comprises returning condensed, solvent-diluent to said reaction zone as a spray, having a drop average particle size of less than 1000 microns, said vaporized solvent-diluent passing through said spray whereby over 50 weight % of said entrained polymer particles of 5 microns and larger are removed from said vaporized solvent-diluent.
Claim 3
Dependent Claim 24 words
The process according to claim 1 wherein the average drop particle size is less than about 600 microns and greater than about 200 microns.
Claim 4
Dependent Claim 20 words
The process according to claim 2 wherein the average drop average particle size is from about 225 to 300 microns.
Claim 5
Dependent Claim 24 words
The process according to claim 1 wherein said spray is produced by a plurality of nozzles in said reaction zone above said liquid phase.
Claim 6
Dependent Claim 22 words
The process according to claim 4 wherein said nozzles are located between said liquid phase and the removal of said vaporized solvent-diluent.
Claim 7
Dependent Claim 17 words
The process according to claim 1 wherein said solvent-diluent is a C 2 to C 8 alpha-olefin.
Claim 8
Dependent Claim 11 words
The process according to claim 6 wherein said alpha-olefin is propylene.

References Cited (Backward Citations)

US3126365A Cited
US3062796A Cited
US3193360A Cited
US3944534A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-11-14 1981-05-16 1981-11-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-11-14 1985-05-16 1985-11-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-11-14 1989-05-16 1989-11-15 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag