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Process for polymerization of butene

Assignee: Mitsui Chemicals Inc
•
Filing: 1979-11-21
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Granted: 1980-12-16
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Expires: 1999-11-21
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Abstract

Abstract A process for the polymerization of butene-1 in a liquid aliphatic hydrocarbon medium in the presence of a catalyst composed of a titanium trihalide and an organoaluminum compound which comprises initially polymerizing a minor part of the butene-1 at a temperature within a range sufficiently low that a slurry of polymer in said medium is produced and then increasing the temperature of polymerization so that the greater part of the butene-1 is polymerized within a high temperature range higher than that of the initial polymerization but not at a temperature so high that the polymer formed dissolves in said medium, characterized in that (1) the initial polymerization is carried out at a temperature of not more than 20 DEG C. in the presence of said titanium trihalide in an amount of not less than 50 millimoles and up to 1,000 millimoles per liter of said medium, and then (2) the polymerization is carried out in the presence or absence of said medium at a temperature of 25 DEG C. to less than 48 DEG C. in the presence of said titanium trihalide in an amount up to one-fifth of that of the initial polymerization.

Inventors

  • 👤 Kunisuke Fukui

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 17:45
CPC Classifications
C; C08; C08F; C08F110/00; C08F110/04; C08F110/08; Y; Y10; Y10S; Y10S526/00; Y10S526/922

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 192 words
In a process for the polymerization of butene-1 in a liquid aliphatic hydrocarbon medium in the presence of a catalyst composed of a titanium trihalide and an organoaluminum compound which comprises initially polymerizing a minor part of the butene-1 at a temperature within a range sufficiently low that a slurry of polymer in said medium is produced and then increasing the temperature of polymerization so that the greater part of the butene-1 is polymerized within a high temperature range higher than that of the initial polymerization but not at a temperature so high that the polymer formed dissolves in said medium; the improvement wherein (1) the initial polymerization is carried out at a temperature of not more than 20° C. in the presence of said titanium trihalide in an amount of not less than 50 millimoles and up to 1,000 millimoles per liter of said medium, and then (2) the polymerization is carried out in the presence or absence of said medium at a temperature of 25° C. to less than 48° C. in the presence of said titanium trihalide in an amount up to one-fifth of that of the initial polymerization.
Claim 2
Dependent Claim 192 words
In a process for the polymerization of butene-1 in a liquid aliphatic hydrocarbon medium in the presence of a catalyst composed of a titanium trihalide and an organoaluminum compound which comprises initially polymerizing a minor part of the butene-1 at a temperature within a range sufficiently low that a slurry of polymer in said medium is produced and then increasing the temperature of polymerization so that the greater part of the butene-1 is polymerized within a high temperature range higher than that of the initial polymerization but not at a temperature so high that the polymer formed dissolves in said medium; the improvement wherein (1) the initial polymerization is carried out at a temperature of not more than 20° C. in the presence of said titanium trihalide in an amount of not less than 50 millimoles and up to 1,000 millimoles per liter of said medium, and then (2) the polymerization is carried out in the presence or absence of said medium at a temperature of 25° C. to less than 48° C. in the presence of said titanium trihalide in an amount up to one-fifth of that of the initial polymerization.
Claim 3
Dependent Claim 43 words
A process according to claim 1 wherein the initial polymerization is carried out so that the amount of polybutene-1 formed is not less than 0.1 g per millimole of titanium and up to 10% by weight of the final polymerization product of butene-1.
Claim 4
Dependent Claim 25 words
A process according to claim 1 wherein the concentration of butene-1 in the initial polymerization is not over 500 millimoles per liter of the medium.

References Cited (Backward Citations)

GB940145A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-12-16 1984-06-16 1984-12-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-12-16 1988-06-16 1988-12-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-12-16 1992-06-16 1992-12-16 $7700.00 Window Closed / Lapsed

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