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US5639834A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing polyethylene having a broad molecular weight distribution

Assignee: TotalEnergies Onetech Belgium SA
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Filing: 1994-10-26
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Granted: 1997-06-17
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Expires: 2014-10-26
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Abstract

Abstract In a process for the copolymerization of ethylene in two liquid full loop reactors in series wherein the average molecular weight is regulated, the introduction of the comonomer is made in the first reactor, and high and low average molecular weight polymers are produced respectively in the first and second reactor, the improvement which consists in using one or more settling legs of the first reactor for the transfer.

Inventors

  • 👤 Guy Debras
  • 👤 Hugo Vandaele

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 08:12
CPC Classifications
C; C08; C08F; C08F10/00; C08F10/02; C08F210/00; C08F210/16

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 255 words
In a process for polymerizing ethylene with at most 20 mole % of one or more alpha-alkenes of 3 to 10 carbon atoms, in two liquid full loop reactors comprising a first and second reactor connected in a series by one or more settling legs of the first reactor connected for discharge of slurry from the first reactor to the second reactor, said process being carried out at a temperature of 50° to 120° C. under an absolute pressure of 1 to 100 bar in the presence of a catalyst, the average molecular weight being regulated, which process comprises carrying out the polymerization such that the introduction of a co-monomer is carried out essentially in the first reactor, that the molecular weight is regulated in the first reactor to form polymers having HLMI between 0.01 and 10 g/10 min., that the residence time in the first reactor is adjusted to produce 30 to 70 wt % of the total polymer and that the molecular weight is regulated in the second reactor to form polymers such that the final polymers have a HLMI higher than 1 g/10 min., the improvement which comprises using one or more settling legs of the first reactor for the transfer to the second reactor wherein the solids content of the slurry in said settling leg is concentrated by gravity settling to a solids concentration that is at least 5 wt % higher than the solids concentration in the first reactor and then discharged from said settling leg to the second reactor.
Claim 2
Dependent Claim 255 words
In a process for polymerizing ethylene with at most 20 mole % of one or more alpha-alkenes of 3 to 10 carbon atoms, in two liquid full loop reactors comprising a first and second reactor connected in a series by one or more settling legs of the first reactor connected for discharge of slurry from the first reactor to the second reactor, said process being carried out at a temperature of 50° to 120° C. under an absolute pressure of 1 to 100 bar in the presence of a catalyst, the average molecular weight being regulated, which process comprises carrying out the polymerization such that the introduction of a co-monomer is carried out essentially in the first reactor, that the molecular weight is regulated in the first reactor to form polymers having HLMI between 0.01 and 10 g/10 min., that the residence time in the first reactor is adjusted to produce 30 to 70 wt % of the total polymer and that the molecular weight is regulated in the second reactor to form polymers such that the final polymers have a HLMI higher than 1 g/10 min., the improvement which comprises using one or more settling legs of the first reactor for the transfer to the second reactor wherein the solids content of the slurry in said settling leg is concentrated by gravity settling to a solids concentration that is at least 5 wt % higher than the solids concentration in the first reactor and then discharged from said settling leg to the second reactor.
Claim 3
Dependent Claim 32 words
The process of claim 1, wherein the contents of the settling leg is transferred whenever it has a solids concentration at least 10 wt % higher than that in the first reactor.
Claim 4
Dependent Claim 32 words
The process of claim 2, wherein the contents of the settling leg is transferred whenever it has a solids concentration at least 20 wt % higher than that in the first reactor.
Claim 5
Dependent Claim 52 words
The process according to any one of claims 1, 2 or 3, wherein the catalyst consists of a transition metal component which is the reaction product of an organomagnesium compound with a titanium compound, an organoaluminium compound and optionally one or more electron donors, the average molecular weight being regulated with hydrogen.
Claim 6
Dependent Claim 16 words
The process according to claim 4, wherein the polymerization temperature is of 60° to 110° C.
Claim 7
Dependent Claim 16 words
The process according to claim 4, wherein the polymerization pressure is of 30 to 50 bar.
Claim 8
Dependent Claim 38 words
The process according to any one of claims 1, 2, 3, 5 and 6, wherein the polymers formed in the first reactor have a HLMI between 0.01 and 5 g/10 min., preferably between 0.1 and 2 g/10 min.
Claim 9
Dependent Claim 25 words
The process according to any one of claims 1, 2, 3 and 5-7, wherein the final polymers have a HLMI higher than 5 g/10 min.
Claim 10
Dependent Claim 23 words
The process according to claim 4, wherein the polymers formed in the first reactor have a HLMI between 0.1 and 2 g/10 min.
Claim 11
Dependent Claim 52 words
The process of claim 4, wherein the transfer of the slurry from the first reactor to the second reactor is carried out employing at least two settling legs, each of which is independently filled with slurry from the first reactor and then concentrated by gravity settling and discharged to the second reactor.

References Cited (Backward Citations)

EP0057420A2 Cited
US4613484A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 2000-06-16 2000-12-16 2001-06-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2004-06-16 2004-12-16 2005-06-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2008-06-16 2008-12-16 2009-06-17 $7700.00 Window Closed / Lapsed

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