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US4098974A Expired / Lapsed US ⏱️ 0.0 years remaining

Polyalkenes of wide molecular weight distribution

Assignee: DSM BV
•
Filing: 1976-07-27
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Granted: 1978-07-04
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Expires: 1996-07-27
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Abstract

Abstract A two-stage cyclical process for producing alkene polymers of wide molecular weight distribution, in which high molecular weight polyalkenes are produced in one stage and lower molecular weight polyalkenes are produced in the other stage and in which polyalkene from one of said stages is introduced into the other of said stages.

Inventors

  • 👤 Dirk Klaassen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 18:13
CPC Classifications
B; B01; B01J; B01J10/00; C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 208 words
A continuous multi-stage process for the suspension polymerization of at least one α-alkene of from 2 to 8 carbon atoms, in the presence of a catalyst comprising at least one compound of at least one transition metal selected from the class consisting of the metals of Groups 4, 5, 6 and 8 of the Periodic Table, and, in the presence of a molecular weight controller, and under pressures of at most 100 kg per cm 2 , and in an inert liquid solvent, which comprises conducting the suspension polymerization reaction in a system of at least two reaction stages, (a) and (b), wherein each such stage employs the same catalyst system, while maintaining the molar ratio of said molecular weight controller to said α-alkene in stage (a) at a level higher than in stage (b), whereby there is formed in stage (a) a polyalkene having a lower average molecular weight than that of the polyalkene formed in stage (b), while also continuously passing polymer suspension formed in reaction stage (a) into reaction stage (b), and while continuously passing polymer suspension formed in stage (b) into stage (a), whereby there is continuously produced a polyalkene having a wide molecular-weight distribution and an ASTM D-1238 melt index of below 100.
Claim 2
Dependent Claim 208 words
A continuous multi-stage process for the suspension polymerization of at least one α-alkene of from 2 to 8 carbon atoms, in the presence of a catalyst comprising at least one compound of at least one transition metal selected from the class consisting of the metals of Groups 4, 5, 6 and 8 of the Periodic Table, and, in the presence of a molecular weight controller, and under pressures of at most 100 kg per cm 2 , and in an inert liquid solvent, which comprises conducting the suspension polymerization reaction in a system of at least two reaction stages, (a) and (b), wherein each such stage employs the same catalyst system, while maintaining the molar ratio of said molecular weight controller to said α-alkene in stage (a) at a level higher than in stage (b), whereby there is formed in stage (a) a polyalkene having a lower average molecular weight than that of the polyalkene formed in stage (b), while also continuously passing polymer suspension formed in reaction stage (a) into reaction stage (b), and while continuously passing polymer suspension formed in stage (b) into stage (a), whereby there is continuously produced a polyalkene having a wide molecular-weight distribution and an ASTM D-1238 melt index of below 100.
Claim 3
Dependent Claim 11 words
Process according to claim 1, wherein said molecular weight-controller is hydrogen.
Claim 4
Dependent Claim 38 words
Process according to claim 1, wherein the molar ratio of hydrogen to alkene in the gaseous phase is between about 75:25 and about 85:15 in stage (a) and said ratio in stage (b) is less than about 25:75.
Claim 5
Dependent Claim 10 words
Process according to claim 3 wherein said alkene is ethylene.
Claim 6
Dependent Claim 27 words
Process according to claim 4 wherein the molar ratio of hydrogen to ethylene in the gaseous phase in stage (b) is between about 10:90 and about 25:75.
Claim 7
Dependent Claim 55 words
The process according to claim 1, wherein a portion of the molecular weight controller is removed from the polymer suspension passing from stage (a) to stage (b) thereby reducing the molar ratio of molecular weight controller to α-alkene to a lower level than the molar ratio of molecular weight controller to α-alkene in stage (a).
Claim 8
Dependent Claim 17 words
Process according to claim 1, wherein the polymerization is carried out at a temperature of 10°-110° C.
Claim 9
Dependent Claim 17 words
Process according to claim 7, wherein the polymerization is carried out at a temperature of 50°-100° C.
Claim 10
Dependent Claim 30 words
Process according to claim 1, wherein when said polymer is introduced to one of the stages (a) or (b), alkene reactants is also introduced to said other of said stages.
Claim 11
Dependent Claim 25 words
Process according to claim 1, wherein said α-alkene is ethylene and the temperature used in stage (a) is higher than the temperature in stage (b).

References Cited (Backward Citations)

GB715666A Cited
US3380978A Cited
US3988395A Cited
US3875128A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-07-03 1982-01-02 1982-07-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-07-03 1986-01-02 1986-07-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-07-03 1990-01-02 1990-07-04 $7700.00 Window Closed / Lapsed

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