US2011130271A1PendingUtilityA1
Ziegler-natta catalyst compositions for producing polyethylenes with a high molecular weight tail and methods of making the same
Est. expiryAug 6, 2028(~2.1 yrs left)· nominal 20-yr term from priority
C08F 2410/03C08F 4/6567C08F 4/6548C08F 210/16C08F 10/00C08F 4/642C08F 4/654C08F 10/02C08F 210/02
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Claims
Abstract
Methods of preparing a polymerization catalyst component is provided, in which a magnesium component, a Lewis acid solubilizing component, a titanium compound, optionally a transition metal compound different than the titanium compound, and typically an inert filler are combined in a slurrying agent and spray-dried to produce a catalyst precursor in the form of a substantially spherical and porous solid particle. The methods and catalysts of this disclosure can provide ethylene homopolymer and copolymer resins having a high molecular weight tail and a broadened molecular weight distribution as compared to more traditional Ziegler-Natta catalysts.
Claims
exact text as granted — not AI-modified1 . A method of preparing a catalyst component, the method comprising:
a) contacting in a slurrying agent:
i) at least one magnesium dihydrocarbyl oxide;
ii) at least one Lewis acidic solubilizing agent; and
iii) at least one titanium compound;
and
b) spray drying the slurry of step a) to evaporate the slurrying agent and to produce solid particles;
where the magnesium dihydrocarbyl oxide and the titanium compound are present in the slurry in any molar ratio.
2 . The method according to claim 1 , where step a) of contacting in a slurrying agent components i), ii), and iii) further comprises contacting with:
iv) at least one transition metal compound different from the titanium compound, where the transition metal is selected from the Groups 4-6 metals.
3 . The method according to claim 2 , where the transition metal compound different from the titanium compound is selected from:
a) Zr(OR 4 ) b Cl 4-b , Hf(OR 4 ) b Cl 4-b , VOCl 3 , or any combination thereof, where b is an integer from 0 to 4, and R 4 in each occurrence is an alkyl group having from 1 to 12 carbon atoms; b) Ti(OR 5 ) c X 1 4-c , or any combination of compounds of this formula, where X 1 is Cl, Br, or I; c is an integer from 0 to 3; and R 5 in each occurrence is an alkyl group having from 1 to 12 carbon atoms; c) TiX 2 d where X 2 is Cl, Br, or I and d is a number from greater than 0 to less than 4; or d) any combination thereof.
4 . The method according to claim 1 , where step a) of contacting in a slurrying agent components i), ii), and iii) further comprises contacting with:
v) a non-porous filler.
5 . The method according to claim 1 , where the slurrying agent is selected from an alcohol having up to 4 carbon atoms or any combination of alcohols having up to 4 carbon atoms.
6 . The method according to claim 1 , where the Lewis acid solubilizing agent is carbon dioxide and the slurrying agent is an alcohol having from 1 to 4 carbon atoms.
7 . The method according to claim 1 , where:
the magnesium dihydrocarbyl oxide has the formula Mg(OR 1 ) 2 where R 1 in each occurrence, is selected independently from an alkyl having up to 6 carbon atoms inclusive; and the Lewis acidic solubilizing agent is selected from carbon dioxide, sulfur dioxide, formaldehyde, Al(OR 2 ) 3 , B(OR 2 ) 3 , or any combination thereof, where R 2 in each occurrence is selected independently from an alkyl having up to 6 carbon atoms inclusive.
8 . The method according to claim 1 , further comprising step c), as follows:
c) contacting the solid particles of step b) with at least one halogenating agent under conditions that partially halogenate the catalyst precursor.
9 . The method according to claim 1 , further comprising step c), as follows:
c) contacting the solid particles of step b) with:
i) at least one mild first halogenating agent and at least one strong second halogenating agent in succession, under conditions which partially halogenate the catalyst precursor; or
ii) at least one strong halogenating agent under conditions which partially halogenate the catalyst precursor.
10 . A catalyst system comprising:
a) a catalyst component prepared according to claim 1 ; b) a halogenating agent; and c) an activating co-catalyst.
11 . The catalyst system according to claim 10 , where the activating co-catalyst is selected from at least one compounds of the formula AlR 10 3 , where R 10 in each occurrence is independently a saturated hydrocarbon groups having from 1 to 14 carbon atoms, optionally substituted with one or more substituents which are inert under the polymerization reaction conditions employed.
12 . A method of preparing a catalyst component, the method comprising:
a) contacting in a slurrying agent:
i) at least one magnesium dihydrocarbyl oxide;
ii) at least one Lewis acidic solubilizing agent;
iii) at least one titanium compound; and
iv) at least one non-porous filler;
b) spray drying the slurry of step a) to evaporate the slurrying agent and to produce solid particles;
and
c) treating the solid particles of step b) with at least one halogenating agent;
where the magnesium dihydrocarbyl oxide, the titanium compound, and the optional transition metal compound different from the titanium compound are present in the slurry in any molar ratio.
13 . The method according to claim 12 , where step a) of contacting in a slurrying agent components i), ii), iii), and iv) further comprises contacting with:
v) at least one transition metal compound different from the titanium compound, where the transition metal is selected from the Groups 4-6 metals.
14 . A catalyst system comprising:
a) catalyst component prepared according to claim 12 ; and b) an activating co-catalyst selected from at least one compounds of the formula AlR 10 3 , where R 10 in each occurrence is independently a saturated hydrocarbon groups having from 1 to 14 carbon atoms, optionally substituted with one or more substituents which are inert under the polymerization reaction conditions employed.
15 . A catalyst component comprising the contact product of:
a) a spray-dried mixture or reaction product of:
i) at least one magnesium dihydrocarbyl oxide;
ii) at least one Lewis acidic solubilizing agent;
iii) at least one titanium compound;
iv) at least one transition metal compound different from the titanium compound, where the transition metal is selected from the Groups 4-6 metals; and
v) at least one non-porous filler;
b) at least one strong second halogenating agent; where contacting occurs under conditions that partially or exhaustively halogenate the spray-dried mixture or reaction product.
16 . The catalyst component according to claim 15 , where the contact product further comprises the contact product of components a) and b) with:
c) at least one mild first halogenating agent.
17 . The catalyst component according to claim 14 , where contacting occurs under conditions that partially halogenate the spray-dried mixture or reaction product.Cited by (0)
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