← Back to Patent Explorer
US4235747A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for improving polymerization performance of brown solid titanium trichloride catalyst component

Assignee: BP Corp North America Inc
•
Filing: 1979-04-19
•
Granted: 1980-11-25
•
Expires: 1999-04-19
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Polymerization performance of organoaluminum reduced, electron donor complexed, brown solid, beta titanium trichloride catalyst component is improved in terms of polymer particle size by contacting said brown solid with at least one aluminum alkyl and at least one alpha-olefin in amounts and under conditions such that a low yield, polyalphaolefin structure is formed around the brown solid.

Inventors

  • 👤 Linus K. Leung

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 22:53
CPC Classifications
C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 28
Claim 1
Independent Claim 487 words
In a process for preparing a brown solid catalyst component comprising beta titanium trichloride and an amount, ranging up to about 10 mole %, of at least one organic electron pair donor compound selected from the group consisting of hydrocarbyl ethers, thioethers, thiols, ketones, esters, amides, amines, phosphines and stibines, said brown solid having a surface area of at least about 50 square meters per gram and a pore volume of at least about 0.10 cc per gram and produced by a process comprising: (a) reacting titanium tetrachloride and at least one organoaluminum component of the formula AlR n X 3-n wherein R is a hydrocarbyl radical, X is chlorine or bromine, and 1<n≦3 in amounts such that the molar ratio of said organoaluminum component to titanium tetrachloride ranges from about 0.5:1 to about 3:1 and at a temperature below about 0° C. in the presence of an inert liquid solvent for said titanium tetrachloride to form a brown solid; (b) increasing the temperature of the brown solid of (a) to less than about 100° C.; (c) contacting the brown solid of (b) with at least one electron pair donor compound selected from the group consisting of hydrocarbyl ethers, thioethers, thiols, ketones, esters, amides, amines, phosphines and stibines in the presence of an inert liquid solvent for said donor compound, the molar ratio of said donor compound to titanium in the brown solid of (b) ranging from about 0.5:1 to about 5:1, and heating at about ambient to about 80° C.; (d) treating the brown solid of (c) with a solution of at least one electron pair acceptor selected from the group consisting of titanium tetrahalides, titanium alkoxyhalides, aluminum bromide, germanium tetrachloride, silicon tetrachloride, and other Group IVA, IVB, and VB halides in an inert liquid at conditions of temperature, time, concentration of said acceptor in said liquid, and molar ratio of said acceptor to titanium contained in said brown solid of (c) which convert said brown solid of (c) into a brown solid having a surface area of above about 50 square meters per gram and a pore volume of above about 0.10 cc per gram; and (e) recovering the solid of (d); the improvement wherein (f) the brown solid from (e) is contacted in the presence of an inert liquid diluent and at a temperature ranging from about 0° to about 40° C. with at least a catalytically effective amount of at least one aluminum alkyl component of the formula AlR' m X 3-m wherein R' is an alkyl radical of 1 to about 20 carbon atoms, X is halogen, and m ranges from 1 to 3, and at least one alpha-olefin at a rate of about 0.05 to about 10 grams alpha-olefin per gram of said brown solid from (e) per hour for a time sufficient to form about 0.005 to about 100 grams solid polyalpha-olefin per gram of said brown solid from (e).
Claim 2
Dependent Claim 487 words
In a process for preparing a brown solid catalyst component comprising beta titanium trichloride and an amount, ranging up to about 10 mole %, of at least one organic electron pair donor compound selected from the group consisting of hydrocarbyl ethers, thioethers, thiols, ketones, esters, amides, amines, phosphines and stibines, said brown solid having a surface area of at least about 50 square meters per gram and a pore volume of at least about 0.10 cc per gram and produced by a process comprising: (a) reacting titanium tetrachloride and at least one organoaluminum component of the formula AlR n X 3-n wherein R is a hydrocarbyl radical, X is chlorine or bromine, and 1<n≦3 in amounts such that the molar ratio of said organoaluminum component to titanium tetrachloride ranges from about 0.5:1 to about 3:1 and at a temperature below about 0° C. in the presence of an inert liquid solvent for said titanium tetrachloride to form a brown solid; (b) increasing the temperature of the brown solid of (a) to less than about 100° C.; (c) contacting the brown solid of (b) with at least one electron pair donor compound selected from the group consisting of hydrocarbyl ethers, thioethers, thiols, ketones, esters, amides, amines, phosphines and stibines in the presence of an inert liquid solvent for said donor compound, the molar ratio of said donor compound to titanium in the brown solid of (b) ranging from about 0.5:1 to about 5:1, and heating at about ambient to about 80° C.; (d) treating the brown solid of (c) with a solution of at least one electron pair acceptor selected from the group consisting of titanium tetrahalides, titanium alkoxyhalides, aluminum bromide, germanium tetrachloride, silicon tetrachloride, and other Group IVA, IVB, and VB halides in an inert liquid at conditions of temperature, time, concentration of said acceptor in said liquid, and molar ratio of said acceptor to titanium contained in said brown solid of (c) which convert said brown solid of (c) into a brown solid having a surface area of above about 50 square meters per gram and a pore volume of above about 0.10 cc per gram; and (e) recovering the solid of (d); the improvement wherein (f) the brown solid from (e) is contacted in the presence of an inert liquid diluent and at a temperature ranging from about 0° to about 40° C. with at least a catalytically effective amount of at least one aluminum alkyl component of the formula AlR' m X 3-m wherein R' is an alkyl radical of 1 to about 20 carbon atoms, X is halogen, and m ranges from 1 to 3, and at least one alpha-olefin at a rate of about 0.05 to about 10 grams alpha-olefin per gram of said brown solid from (e) per hour for a time sufficient to form about 0.005 to about 100 grams solid polyalpha-olefin per gram of said brown solid from (e).
Claim 3
Dependent Claim 64 words
The process of claim 1 wherein the organoaluminum component in (a) is a trialkylaluminum, a dialkylaluminum chloride, a mixture thereof, or a mixture of a dialkylaluminum chloride with an alkylaluminum dichloride in amounts such that the total chlorine to aluminum molar ratio is greater than 1 and no greater than about 1.5, each of said alkyl radicals containing 1 to about 8 carbon atoms.
Claim 4
Dependent Claim 16 words
The process of claim 2 wherein the electron pair donor compound in (c) is diisoamyl ether.
Claim 5
Dependent Claim 17 words
The process of claim 1 wherein the electron pair donor compound in (c) is a dialkyl ether.
Claim 6
Dependent Claim 17 words
The process of claim 4 wherein the organoaluminum component in (a) is diethylaluminum chloride or ethylaluminum sesquichloride.
Claim 7
Dependent Claim 15 words
The process of claim 1 wherein the electron pair acceptor in (d) is titanium tetrachloride.
Claim 8
Dependent Claim 28 words
The process of claim 6 wherein the organoaluminum component in (a) is diethylaluminum chloride or ethylaluminum sesquichloride and the electron pair donor compound in (b) is diisoamyl ether.
Claim 9
Dependent Claim 12 words
The process of claim 7 wherein the alpha-olefin in (f) is propylene.
Claim 10
Dependent Claim 15 words
The process of claim 8 wherein the aluminum alkyl component in (f) is diethylaluminum chloride.
Claim 11
Dependent Claim 12 words
The process of claim 1 wherein the alpha-olefin in (f) is propylene.
Claim 12
Dependent Claim 14 words
The process of claim 10 wherein the aluminum alkyl in (f) is diethylaluminum chloride.
Claim 13
Dependent Claim 15 words
The low yield-polypropylene-encapsulated brown solid catalyst component obtained according to the process of claim 11.
Claim 14
Dependent Claim 15 words
The low yield-polyalpha-olefin-encapsulated brown solid catalyst component obtained according to the process of claim 1.
Claim 15
Dependent Claim 154 words
A process for improving the alpha-olefin polymerization performance of organoaluminum reduced, electron donor complexed, brown solid, beta titanium trichloride catalyst component in terms of polymer particle size and decreasing the initial polymerization activity of said component without substantially decreasing overall polymerization activity comprising contacting said brown solid in the presence of an inert liquid diluent and at a temperature ranging from about 0° to about 40° C. with at least a catalytically effective amount of at least one aluminum alkyl component of the formula AlR' m X 3-m wherein R' is an alkyl radical of 1 to about 20 carbon atoms, X is halogen, and m ranges from 1 to 3, and at least one alpha-olefin at a rate of about 0.05 to about 10 grams alpha-olefin per gram of brown solid per hour for a time sufficient to form about 0.005 to about 100 grams solid polyalpha-olefin per gram of said brown solid.
Claim 16
Dependent Claim 154 words
A process for improving the alpha-olefin polymerization performance of organoaluminum reduced, electron donor complexed, brown solid, beta titanium trichloride catalyst component in terms of polymer particle size and decreasing the initial polymerization activity of said component without substantially decreasing overall polymerization activity comprising contacting said brown solid in the presence of an inert liquid diluent and at a temperature ranging from about 0° to about 40° C. with at least a catalytically effective amount of at least one aluminum alkyl component of the formula AlR' m X 3-m wherein R' is an alkyl radical of 1 to about 20 carbon atoms, X is halogen, and m ranges from 1 to 3, and at least one alpha-olefin at a rate of about 0.05 to about 10 grams alpha-olefin per gram of brown solid per hour for a time sufficient to form about 0.005 to about 100 grams solid polyalpha-olefin per gram of said brown solid.
Claim 17
Dependent Claim 24 words
The process of claim 14 wherein the aluminum alkyl component is a dialkylaluminum chloride containing 2 to about 8 carbon atoms per alkyl radical.
Claim 18
Dependent Claim 10 words
The process of claim 15 wherein the alpha-olefin is propylene.
Claim 19
Dependent Claim 12 words
The process of claim 16 wherein the dialkylaluminum chloride is diethylaluminum chloride.
Claim 20
Dependent Claim 16 words
The process of claim 17 wherein the temperature ranges from about 10° to about 35° C.
Claim 21
Dependent Claim 15 words
The low yield-polypropylene-encapsulated brown solid catalyst component obtained according to the process of claim 18.
Claim 22
Dependent Claim 15 words
The low yield-polyalpha-olefin-encapsulated brown solid catalyst component obtained according to the process of claim 14.
Claim 23
Dependent Claim 56 words
The process of claim 14 further characterized in that said brown solid, aluminum alkyl component, and alpha-olefin are contacted in the presence of at least one crystallinity promoting component which is present in an amount which is effective to improve the polymerization performance of said brown solid in terms of stereospecificity without substantial decreases in activity.
Claim 24
Dependent Claim 29 words
The process of claim 21 wherein the alpha-olefin is propylene and the aluminum alkyl component is a dialkylaluminum chloride containing 2 to about 8 carbon atoms per alkyl radical.
Claim 25
Dependent Claim 12 words
The process of claim 22 wherein the dialkylaluminum chloride is diethylaluminum chloride.
Claim 26
Dependent Claim 16 words
The process of claim 23 wherein the temperature ranges from about 10° to about 35° C.
Claim 27
Dependent Claim 15 words
The low yield-polypropylene-encapsulated brown solid catalyst component obtained according to the process of claim 24.
Claim 28
Dependent Claim 15 words
The low yield-polyalpha-olefin-encapsulated brown solid catalyst component obtained according to the process of claim 21.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-11-25 1984-05-26 1984-11-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-11-25 1988-05-26 1988-11-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-11-25 1992-05-26 1992-11-25 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag