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Process for the production of a catalyst component for use in the polymerization of α-olefins

Assignee: Tonen General Sekiyu KK
•
Filing: 1976-07-06
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Granted: 1977-12-20
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Expires: 1996-07-06
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Abstract

Abstract This invention relates to a catalyst composition for polymerization of propylene, having high activity and producing polypropylene of high stereoregularity and having a low particle size distribution, which comprises; 1. REDUCING TiCl4 by diethylaluminum chloride (DEAC), thereby forming a reduced solid (TiCl3), 2. REMOVING THE ALUMINUM COMPOUNDS FROM THE REDUCED CATALYST, 3. TREATING THE SAID REDUCED SOLID WITH THE MIXTURE OR COMPLEX OF TiCl4 and diisoamylether (IAE) and 4. SEPARATING THE SOLID CATALYST FROM THE MIXTURE.

Inventors

  • 👤 Hiroshi Ueno
  • 👤 Naomi Inaba
  • 👤 Tokuo Makishima
  • 👤 Shozo Wada

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 10:12
CPC Classifications
C; C08; C08F; C08F10/00; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 175 words
A process for the production of a catalyst component for use in polymerization of alpha-olefins which comprises: reducing titanium tetrachloride with an organoaluminum compound having the general formula AlR n x 3-n wherein R represents a hydrocarbon group having 1 to 18 carbon atoms, X represents a halogen, and n represents a number expressed as 0 < n ≦ 3 to obtain a brown or black-brown titanium trichloride reduced solid containing aluminum compounds; removing aluminum compounds from said brown or black-brown titanium trichloride reduced solid; and thereafter contacting said brown or black-brown titanium trichloride reduced solid in an inert diluent with an activator selected from the group consisting of a complex of diisoamyl ether and titanium tetrachloride, and a mixture of diisoamyl ether and titanium tetrachloride at a temperature within the range of from -30° to 100° C for at least 30 minutes, wherein the mole ratio of diisoamyl ether to titanium trichloride is at least 0.1 and the concentration of titanium tetrachloride in the liquid phase is maintained at at least 1 volume percent.
Claim 2
Dependent Claim 175 words
A process for the production of a catalyst component for use in polymerization of alpha-olefins which comprises: reducing titanium tetrachloride with an organoaluminum compound having the general formula AlR n x 3-n wherein R represents a hydrocarbon group having 1 to 18 carbon atoms, X represents a halogen, and n represents a number expressed as 0 < n ≦ 3 to obtain a brown or black-brown titanium trichloride reduced solid containing aluminum compounds; removing aluminum compounds from said brown or black-brown titanium trichloride reduced solid; and thereafter contacting said brown or black-brown titanium trichloride reduced solid in an inert diluent with an activator selected from the group consisting of a complex of diisoamyl ether and titanium tetrachloride, and a mixture of diisoamyl ether and titanium tetrachloride at a temperature within the range of from -30° to 100° C for at least 30 minutes, wherein the mole ratio of diisoamyl ether to titanium trichloride is at least 0.1 and the concentration of titanium tetrachloride in the liquid phase is maintained at at least 1 volume percent.
Claim 3
Dependent Claim 18 words
A process according to claim 1 wherein the aluminum compounds are removed by washing with a complexing agent.
Claim 4
Dependent Claim 28 words
A process according to claim 2 wherein the complexing agent is selected from the group consisting of ethers, thioethers, thiols, organo-phosphorus compounds, organo nitrogen compounds, ketones and esters.
Claim 5
Dependent Claim 13 words
A process according to claim 3 wherein the complexing agent is di-n-butyl ether.
Claim 6
Dependent Claim 18 words
A process according to claim 1 wherein the activator is a complex of diisoamyl ether and titanium tetrachloride.
Claim 7
Dependent Claim 18 words
A process according to claim 1 wherein the activator is a mixture of diisoamyl ether and titanium tetrachloride.
Claim 8
Dependent Claim 70 words
A process according to claim 1, wherein, in said contacting of brown or black-brown titanium trichloride reduced solid in inert diluent with said activator, the mole ratio of diisoamyl ether to titanium trichloride is within the range of 0.1 to 0.6, the concentration of titanium tetrachloride in the diluent is at least 5 volume percent and the reduced solid concentration in the diluent is at least 50 grams per liter.

References Cited (Backward Citations)

US3769233A Cited
US3825524A Cited
US3862257A Cited
US3960765A Cited
US3984350A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-12-19 1981-06-20 1981-12-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-12-19 1985-06-20 1985-12-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-12-19 1989-06-20 1989-12-20 $7700.00 Window Closed / Lapsed

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