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US4153774A Expired / Lapsed US ⏱️ 0.0 years remaining

Manufacture of high pressure polyethylene

Assignee: BASF SE
•
Filing: 1977-11-10
•
Granted: 1979-05-08
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Expires: 1997-11-10
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Abstract

Abstract A process for the high pressure polymerization of ethylene at elevated temperatures in a polymerization zone followed by transfer of the reaction mixture, through a cooling zone, into the separation zone. In this process, the pressure at the cooling zone outlet is periodically reduced briefly, at recurring intervals, these brief pressure reductions being independent of the pressure reductions in the polymerization zone. Using this process, the conversion in the polymerization unit can be increased and a more homogeneous ethylene polymer can be obtained.

Inventors

  • 👤 Klaus Boettcher
  • 👤 Heinrich G. Hoerdt
  • 👤 Wieland Zacher
  • 👤 Oskar Buechner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 11:57
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/26; Y; Y10; Y10S; Y10S526/00; Y10S526/921

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 156 words
A process for the continuous manufacture of an ethylene polymer by homopolymerization of ethylene or copolymerization of ethylene with one or more other monomers copolymerizable with ethylene, in a polymerization zone at from 1,000 to 4,000 bars and from 100° to 450° C., followed by transfer of the reaction mixture through a cooling zone into a high pressure product separation zone where the pressure is from 200 to 350 bars, the pressure prevailing in the cooling zone being lower than in the polymerization zone but being from 50 to 500 bars higher than in the high pressure product separation zone, wherein the pressure in the cooling zone is reduced periodically and recurrently for a duration of from 0.1 to 10 seconds at the outlet from the cooling zone to the high pressure product separation zone, these brief pressure reductions being independent of the pressure reductions to which the reaction mixture is subjected in the polymerization zone.
Claim 2
Dependent Claim 156 words
A process for the continuous manufacture of an ethylene polymer by homopolymerization of ethylene or copolymerization of ethylene with one or more other monomers copolymerizable with ethylene, in a polymerization zone at from 1,000 to 4,000 bars and from 100° to 450° C., followed by transfer of the reaction mixture through a cooling zone into a high pressure product separation zone where the pressure is from 200 to 350 bars, the pressure prevailing in the cooling zone being lower than in the polymerization zone but being from 50 to 500 bars higher than in the high pressure product separation zone, wherein the pressure in the cooling zone is reduced periodically and recurrently for a duration of from 0.1 to 10 seconds at the outlet from the cooling zone to the high pressure product separation zone, these brief pressure reductions being independent of the pressure reductions to which the reaction mixture is subjected in the polymerization zone.
Claim 3
Dependent Claim 22 words
The process of claim 1, wherein the magnitude of the pressure reductions in the cooling zone is from 50 to 500 bars.
Claim 4
Dependent Claim 37 words
The process of claim 1, wherein the time interval between the end of one pressure reduction and the start of the next pressure reduction in the cooling zone is in each case from 5 to 500 seconds.
Claim 5
Dependent Claim 25 words
The process of claim 1 or 3, wherein the residence time of the reaction mixture in the cooling zone is from 5 to 200 seconds.

References Cited (Backward Citations)

GB1047851A Cited
US3784538A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-05-07 1982-11-06 1983-05-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-05-07 1986-11-06 1987-05-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-05-07 1990-11-06 1991-05-08 $7700.00 Window Closed / Lapsed

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