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US4200717A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of propylene polymer-containing solid titanium trichloride and propylene polymers using same

Assignee: Mitsubishi Chemical Corp
•
Filing: 1978-03-27
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Granted: 1980-04-29
•
Expires: 1998-03-27
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Abstract

Abstract A solid titanium trichloride, produced by precipitation from a homogeneous solution or mixture with an ether, is treated by prepolymerization with propylene at a partial pressure of less than 1 kg/cm2. The pretreated titanium trichloride containing a propylene polymer is then admixed with an organoaluminum compound and the admixture is used as a catalyst in the polymerization of propylene.

Inventors

  • 👤 Toshizo Abe
  • 👤 Nobuaki Goko
  • 👤 Yasuhiro Nishihara
  • 👤 Yukimasa Matuda

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 14:46
CPC Classifications
C; C08; C08F; C08F10/00; C08F10/04; C08F10/06; Y; Y10; Y10S; Y10S526/00; Y10S526/903; Y10S526/904; Y10S526/907

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 152 words
A solid titanium trichloride catalyst containing a polymer of propylene produced by the process comprising: (a) forming a homogeneous solution comprising titanium trichloride and an ether; (b) heating said homogeneous solution at a temperature of lower than 150° C. to form a precipitate of solid titanium trichloride; (c) separating said precipitate; (d) mixing said separated precipitate, an inert solvent and an organoaluminum compound in a closed vessel; and (e) introducing propylene into said vessel for absorption into the liquid phase in said vessel at a feed rate within the range of 1 to 10 grams per hour per gram of said solid titanium trichloride, maintaining the partial pressure of said propylene in the gaseous phase in said vessel at less than 1 kg/cm 2 , the amount of propylene so introduced being controlled so that the amount of propylene absorbed is 0.1 to 50 times the weight of said solid titanium trichloride.
Claim 2
Dependent Claim 152 words
A solid titanium trichloride catalyst containing a polymer of propylene produced by the process comprising: (a) forming a homogeneous solution comprising titanium trichloride and an ether; (b) heating said homogeneous solution at a temperature of lower than 150° C. to form a precipitate of solid titanium trichloride; (c) separating said precipitate; (d) mixing said separated precipitate, an inert solvent and an organoaluminum compound in a closed vessel; and (e) introducing propylene into said vessel for absorption into the liquid phase in said vessel at a feed rate within the range of 1 to 10 grams per hour per gram of said solid titanium trichloride, maintaining the partial pressure of said propylene in the gaseous phase in said vessel at less than 1 kg/cm 2 , the amount of propylene so introduced being controlled so that the amount of propylene absorbed is 0.1 to 50 times the weight of said solid titanium trichloride.
Claim 3
Dependent Claim 22 words
The solid propylene polymer-containing titanium trichloride of claim 1, produced by the process wherein the homogeneous solution further comprises a hydrocarbon solvent.
Claim 4
Dependent Claim 25 words
The propylene polymer-containing solid titanium trichloride of claim 1, produced by the process wherein the propylene is injected into the liquid phase within the vessel.
Claim 5
Dependent Claim 32 words
The propylene polymer-containing solid titanium trichloride of claim 3, produced by the process wherein the partial pressure of propylene in the gaseous phase is maintained at less than 0.2 kg/cm 2 .
Claim 6
Dependent Claim 24 words
The propylene polymer-containing solid titanium trichloride of claim 1, produced by the process wherein propylene is supplied into the gaseous phase in the vessel.
Claim 7
Dependent Claim 32 words
The propylene polymer-containing solid titanium trichloride of claim 5, produced by the process wherein the partial pressure of propylene in the gaseous phase is maintained at less than 0.6 kg/cm 2 .
Claim 8
Dependent Claim 23 words
The propylene polymer-containing solid titanium trichloride of claim 1, produced by the process wherein substantially no hydrogen is present within the reaction vessel.
Claim 9
Dependent Claim 26 words
The propylene polymer-containing solid titanium trichloride of claim 1, produced by the process wherein the propylene is supplied at a temperature of 0° to 70° C.
Claim 10
Dependent Claim 40 words
The propylene polymer-containing solid titanium trichloride of claim 1, produced by a process further comprising the steps of separating the propylene polymer-containing solid titanium trichloride produced in step (d) from the liquid phase and then washing with an inert solvent.
Claim 11
Dependent Claim 28 words
A propylene polymer-containing solid titanium trichloride of claim 1, produced by a process wherein the propylene is introduced with a small amount of at least one other α-olefin.
Claim 12
Dependent Claim 37 words
In a method of producing a propylene polymer the improvement comprising polymerizing the propylene in the presence of a catalyst admixture of (a) the propylene polymer-containing solid titanium trichloride of claim 1, and (b) an organoaluminum compound.
Claim 13
Dependent Claim 28 words
The method of claim 11, wherein the propylene is polymerized together with a small quantity of at least one other α-olefin in the presence of said catalyst admixture.
Claim 14
Dependent Claim 24 words
The method of claim 11, wherein propylene is polymerized at a temperature of 50° to 90° C. in the presence of said catalyst admixture.
Claim 15
Dependent Claim 28 words
The method of claim 11, wherein the propylene is polymerized under a partial pressure of propylene of 1 to 100 atm. in the presence of said catalyst admixture.
Claim 16
Dependent Claim 32 words
The method of claim 11, wherien the propylene polymer is produced in a yield of more than 5,000 times the weight of solid titanium trichloride in the presence of said catalyst admixture.
Claim 17
Dependent Claim 156 words
A process for producing a solid titanium trichloride containing a polymer of propylene comprising the steps of: (a) forming a homogeneous solution comprising titanium trichloride and an ether; (b) heating said homogeneous solution at a temperature of lower than 150° C. to form a precipitate of solid titanium trichloride; (c) separating said precipitate; (d) mixing said separated solid titanium trichloride, an inert solvent and an organoaluminum compound in a closed vessel; and (e) introducing propylene into said vessel for absorption into the liquid phase in said vessel at a feed rate within the range of 1 to 10 grams per hour per gram of said solid titanium trichloride, maintaining the partial pressure of said propylene in the gaseous phase in said vessel at less than 1 kg/cm 2 , the amount of propylene so introduced being controlled so that the amount of propylene absorbed is 0.1 to 50 times the weight of said solid titanium trichloride.
Claim 18
Dependent Claim 156 words
A process for producing a solid titanium trichloride containing a polymer of propylene comprising the steps of: (a) forming a homogeneous solution comprising titanium trichloride and an ether; (b) heating said homogeneous solution at a temperature of lower than 150° C. to form a precipitate of solid titanium trichloride; (c) separating said precipitate; (d) mixing said separated solid titanium trichloride, an inert solvent and an organoaluminum compound in a closed vessel; and (e) introducing propylene into said vessel for absorption into the liquid phase in said vessel at a feed rate within the range of 1 to 10 grams per hour per gram of said solid titanium trichloride, maintaining the partial pressure of said propylene in the gaseous phase in said vessel at less than 1 kg/cm 2 , the amount of propylene so introduced being controlled so that the amount of propylene absorbed is 0.1 to 50 times the weight of said solid titanium trichloride.

References Cited (Backward Citations)

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US3332925A Cited
US3575948A Cited
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US3864278A Cited
GB1408620A Cited
US4007133A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-29 1983-10-29 1984-04-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-29 1987-10-29 1988-04-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-29 1991-10-29 1992-04-29 $7700.00 Window Closed / Lapsed

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