Plaque It!
Sponsored by: Flash of Genius |
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The present invention relates to a supported, treated catalyst system and its use in a process for polymerizing olefin(s). In particular, the invention is directed to a supported, treated catalyst system that includes a supported bimetallic catalyst system that has been contacted with at least one methylalumoxane-activatable compound, and polymerization process employing such a supported, treated catalyst system.
Advances in polymerization and catalysis have resulted in the ability to produce many new polymers having improved physical and chemical properties useful in a wide variety of superior products and applications. The development of new catalysts has greatly expanded the choice of polymerization processes (solution, slurry, high pressure or gas phase) for producing a particular polymer. Also, advances in polymerization technology have provided more efficient, highly productive and economically enhanced processes. Especially illustrative of these advances is the development of the technology field utilizing metallocene catalyst systems.
As with any new technology field, particularly in the polyolefins industry, a small savings in cost often determines whether a commercial endeavor is even feasible. This aspect of the metallocene technology field is evident by the number of participants in the industry seeking new ways to reduce cost. In particular, there has been tremendous focus in the industry on developing new and improved metallocene catalyst systems. Some have focused on designing the catalyst systems to produce new polymers, others on improved operability, and many more on improving catalyst productivity. The productivity of a catalyst, that is, the amount of polymer produced per gram of the catalyst per hour, usually is the key economic factor that can make or break a new commercial development in the polyolefins industry.
From the early stages in the metallocene technology field, beginning with the discovery of the utility of alumoxane as a cocatalyst in the early 1980's, to the discovery of substitutions on the ligands of the metallocene compounds, through the development of non-coordinating anions, and today with the ever-increasing number of new metallocene compounds, catalyst productivity has been a primary focus.
A need still exists for higher productivity catalyst systems capable of providing the efficiencies necessary for implementing commercial polyolefin processes. Further, it has been found that conventional olefin polymerization processes that employ catalyst systems that use methylalumoxane as an activator often fail to efficiently utilize all the methylalumoxane present in the catalyst system. This is problematic because methylalumoxane represents a significant cost factor in the catalyst system. Thus, it would be highly advantageous to have a polymerization process and catalyst system capable of producing polyolefins with improved catalyst productivities and improved methylalumoxane efficiency.
The present invention relates to a supported, treated catalyst system and its use in a process for polymerizing olefin(s). In particular, the invention is directed to a supported, treated catalyst system that includes a supported bimetallic catalyst system that has been contacted with at least one methylalumoxane-activatable compound.
In one exemplary embodiment, the present invention provides a process for polymerizing olefins by contacting, in a reactor: (a) ethylene and at least one comonomer selected from the group consisting of C4 to C8 alpha olefins; and (b) a supported, treated catalyst system that includes a first catalyst component, a second catalyst component, and at least one methylalumoxane-activatable compound.
In another exemplary embodiment, a supported, treated catalyst system is produced by a process comprising the steps of: (a) forming a supported bimetallic catalyst system comprising a first catalyst component and a second catalyst component; and (b) contacting the supported bimetallic catalyst system with at least one methylalumoxane-activatable compound.
A more complete understanding of the present disclosure and advantages thereof may be acquired by referring to the following description taken in conjunction with the accompanying drawings, wherein:
FIG. 1 illustrates a molecular weight distribution for an exemplary supported bimetallic catalyst composition.
FIG. 2 illustrates a molecular weight distribution for an exemplary supported, treated catalyst system of the present invention.
FIG. 3 illustrates a molecular weight distribution for an exemplary supported, treated catalyst system of the present invention.
FIG. 4 illustrates a molecular weight distribution for an exemplary supported, treated catalyst system of the present invention.
FIG. 5 illustrates a molecular weight distribution for an exemplary supported, treated catalyst system of the present invention.
FIG. 6 illustrates a molecular weight distribution for an exemplary supported, treated catalyst system of the present invention.
General Definitions
As used herein, in reference to Periodic Table “Groups” of Elements, the “new” numbering scheme for the Periodic Table Groups is used, as in the CRC H
As used herein, the phrase “catalyst system” includes at least one “catalyst component” and at least one “activator,” both of which are described further herein. The catalyst system may also include other components (such as supports, for example), and is not limited to the catalyst component and/or activator alone, or in combination. The catalyst system may include any number of catalyst components, in any combination as described herein, and may also include any activator in any combination as described herein. In one embodiment of the present invention, a “supported, treated catalyst system” is provided that includes a “bimetallic catalyst system” that has been contacted with at least one compound that can be activated by methylalumoxane (“MAO-activatable compound”).
As used herein, the term “bimetallic catalyst” or “bimetallic catalyst system” refers to two or more catalyst components that may be used in combination with at least one activator and a support material.
As used herein, the phrase “catalyst compound” includes any compound that, once appropriately activated, is capable of catalyzing the polymerization or oligomerization of olefins, the catalyst compound including at least one Group 3 to Group 12 atom, and optionally at least one leaving group bound thereto.
As used herein, the phrase “leaving group” refers to one or more chemical moieties bound to the metal center of the catalyst component, which can be abstracted from the catalyst component by an activator, thus producing a species active towards olefin polymerization or oligomerization. The activator is described further below.
As used herein, the term “substituted” means that the group following that term possesses at least one moiety in place of one or more hydrogens in any position, which moieties are selected from such groups as halogen radicals (e.g., Cl, F, Br), hydroxyl groups, carbonyl groups, carboxyl groups, amine groups, phosphine groups, alkoxy groups, phenyl groups, naphthyl groups, C1 to C10 alkyl groups, C2 to C10 alkenyl groups, and combinations thereof. Examples of substituted alkyls and aryls include, but are not limited to, acyl radicals, alkylamino radical, alkoxy radicals, aryloxy radicals, alkylthio radicals, dialkylamino radicals, alkoxycarbonyl radicals, aryloxycarbonyl radicals, carbomoyl radicals, alkyl- and dialkyl-carbomoyl radicals, acyloxy radicals, acylamino radicals, arylamino radicals, and combinations thereof.
As used herein, structural formulas are employed in manners that are commonly understood in the chemical arts. For example, the lines (“- - ”) that are used to represent associations between a metal atom (“M,” Group 3 to Group 12 atoms) and a ligand or ligand atom (e.g., cyclopentadienyl, nitrogen, oxygen, halogen ions, alkyl, etc.), as well as the phrases “associated with,” “bonded to” and “bonding,” are not limited to representing a certain type of chemical bond; rather, these lines and phrases are meant to represent a “chemical bond” in general. As used herein, the phrase “chemical bond” is defined as an attractive force between atoms that is strong enough to permit the combined aggregate to function as a unit, or “compound.”
A certain stereochemistry for a given structure or part of a structure should not be implied unless so stated for a given structure or apparent by use of commonly used bonding symbols, such as by dashed lines and/or heavy lines.
Unless stated otherwise, no embodiment of the present invention is herein limited to the oxidation state of the metal atom “M” as defined below in the individual descriptions and examples that follow. The ligation of the metal atom “M” is such that the compounds described herein are neutral, unless otherwise indicated.
As used herein, the term “bimodal,” when used to describe a polymer or polymer composition (e.g., polyolefins such as polypropylene or polyethylene, or other homopolymers, copolymers or terpolymers) means “bimodal molecular weight distribution,” which is understood as having the broadest definition persons in the pertinent art have given that term as reflected in printed publications and issued patents. For example, a single composition that includes polyolefins with at least one identifiable high molecular weight distribution and polyolefins with at least one identifiable low molecular weight distribution is considered to be a “bimodal” polyolefin, as that term is used herein. In a particular embodiment, other than having different molecular weights, the high molecular weight polyolefin and the low molecular weight polyolefin may be essentially the same type of polymer, for example, polyethylene.
As used herein, the term “productivity” means the weight of polymer produced per weight of the catalyst used in the polymerization process per time period (e.g., grams polymer/(gram catalyst·hour).
As used herein, the term “dehydrated” is understood as having the broadest definition that persons in the pertinent art have given that term in describing catalyst support materials (for example, silica) as reflected in printed publications and issued patents, and includes any material (for example, a support particle) from which a majority of the contained/adsorbed water has been removed.
As used herein, the term “MAO efficiency” refers to the grams of polyethylene produced per mmol aluminum (contributed by MAO) present on the supported (or supported, treated) catalyst per hour when the supported (or supported, treated) catalyst system is used in a polymerization process.
Bimetallic Catalyst
As used herein, the term “supported bimetallic catalyst” or “supported bimetallic catalyst composition” refers to a bimetallic catalyst system as used in combination with a support material, wherein one or more of the components that make up the bimetallic catalyst system may be bound to the support. In a particular embodiment, the bimetallic catalyst used in accordance with the present invention includes two catalyst components. In a more particular embodiment, the bimetallic catalyst includes a “first catalyst component” and a “second catalyst component.”
As used herein, the term “first catalyst component” refers to any catalyst component other than the second catalyst component. In certain exemplary embodiments, the first catalyst component is a non-metallocene catalyst component, examples of which include, but are not limited to, titanium or vanadium based Ziegler-Natta catalyst compounds as described further herein. In an exemplary embodiment, the first catalyst component is titanium tetrachloride.
As used herein, the term “non-metallocene catalyst component” refers to any catalyst component that is neither a metallocene nor one of the metallocene-type catalyst compounds identified below.
As used herein, the term “second catalyst component” refers to any catalyst component that is different from a first catalyst component. In an exemplary embodiment, the second catalyst component is a metallocene catalyst component.
In an exemplary embodiment, each different catalyst compound that comprises the bimetallic catalyst resides, or is supported, on a single type of support such that, on average, each particle of support material includes both the first and second catalyst components. In another exemplary embodiment, the first catalyst component is supported separately from the second catalyst component such that, on average, any given particle of support material comprises only the first or the second catalyst component. In this later embodiment, each supported catalyst component may be introduced into the polymerization reactor sequentially in any order, alternately in parts, or simultaneously.
In a particular embodiment, the first catalyst component includes a titanium non-metallocene catalyst component, from which a higher molecular weight resin (e.g., >ca 100,000 amu) can be produced. In a particular embodiment, the second catalyst component includes a metallocene component, from which a lower molecular weight resin (e.g., <ca 100,000 amu) can be produced. Accordingly, when such bimetallic catalyst is included in the supported, treated catalyst systems of the present invention, polymerization in the presence of such supported, treated catalyst system may provide a bimodal polyolefin composition that includes a low molecular weight component and a high molecular weight component.
In one exemplary embodiment, an “enhanced silica” is prepared as described herein and constitutes the support for the bimetallic catalyst. In an exemplary embodiment, the first catalyst component is a non-metallocene compound that is first combined with the enhanced silica, to provide a supported non-metallocene composition that is combined with the second catalyst component.
Various methods of affixing two different catalyst components (albeit a different combination of catalysts) to a support can be used. One procedure for preparing a supported bimetallic catalyst can include providing a supported first catalyst component, contacting a slurry that includes the first catalyst component in a non-polar hydrocarbon with a solution that includes the second catalyst component, which may also include an activator, drying the resulting product that includes the first and second catalyst components, and recovering a supported bimetallic catalyst composition. The present invention is not limited to any particular method of affixing the catalyst components to the support.
First Catalyst Component
As noted above, exemplary embodiments of the bimetallic catalyst composition useful in the supported, treated catalyst systems of the present invention may include a first catalyst component, which is, or may include, a non-metallocene compound. However, it is contemplated that for certain applications the first catalyst component may alternatively be a metallocene compound, or even one of the metallocene-type catalyst compounds identified below that is different in structure from the second catalyst component as described herein. In a particular embodiment, the first catalyst component is a Ziegler-Natta catalyst compound. Ziegler-Natta catalyst components are well known in the art and described by, for example, Z
The first catalyst component is combined with a support material, in one exemplary embodiment, either with, or without, the second catalyst component. The first catalyst component can be combined with, placed on, or otherwise affixed to a support in a variety of ways. In one of those ways, a slurry of the support in a suitable non-polar hydrocarbon diluent is contacted with an organomagnesium compound, which then dissolves in the non-polar hydrocarbon diluent of the slurry to form a solution from which the organomagnesium compound is then deposited onto the carrier. The organomagnesium compound can be represented by the formula RMgR′, where R′ and R are the same or different C2-C12 alkyl groups, or C4-C10 alkyl groups, or C4-C8 alkyl groups. In one exemplary embodiment, the organomagnesium compound is dibutyl magnesium. In one exemplary embodiment, the amount of organomagnesium compound included in the silica slurry is essentially only that which will be deposited, physically or chemically, onto the support (for example, being bound to the hydroxyl groups on the support) and essentially no more than that amount, as any excess organomagnesium compound may cause undesirable side reactions. Routine experimentation can be used to determine the optimum amount of organomagnesium compound. For example, the organomagnesium compound can be added to the slurry while stirring the slurry, until the organomagnesium compound is detected in the support solvent. Alternatively, the organomagnesium compound can be added in excess of the amount that is deposited onto the support, in which case any undeposited excess amount can be removed by filtration and washing. The amount of organomagnesium compound (moles) based on the amount of dehydrated silica (grams) generally ranges from 0.2 mmol/gram to 2 mmol/gram, in one exemplary embodiment.
Optionally, the organomagnesium compound-treated slurry may be contacted with an electron donor, such as tetraethylorthosiloxane (TEOS) or an organic alcohol R″OH, where R″ is a C1-C12 alkyl group, or a C1 to C8 alkyl group, or a C2 to C4 alkyl group. In a particular embodiment, R″OH is n-butanol. The amount of alcohol used may be an amount effective to provide an R″OH:Mg mol/mol ratio of from 0.2 to 1.5, or from 0.4 to 1.2, or from 0.6 to 1.1, or from 0.9 to 1.0.
In an exemplary embodiment, the organomagnesium-and-alcohol-treated slurry is contacted with a non-metallocene transition metal compound. Suitable non-metallocene transition metal compounds are, for example, compounds of Group 4 and 5 metals that are soluble in the non-polar hydrocarbon used to form the silica slurry. Suitable non-metallocene transition metal compounds include, for example, titanium and vanadium halides, oxyhalides or alkoxyhalides, such as titanium tetrachloride (TiCl4), vanadium tetrachloride (VCl4) and vanadium oxytrichloride (VOCl3), and titanium and vanadium alkoxides, wherein the alkoxide moiety has a branched or unbranched alkyl group of 1 to 20 carbon atoms, preferably 1 to 6 carbon atoms. Mixtures of such transition metal compounds also may be used. The amount of non-metallocene transition metal compound used is sufficient to give a molar ratio of transition metal to magnesium of from 0.3 to 1.5, or from 0.5 to 0.8 in a particular exemplary embodiment. The diluent can then be removed in a conventional manner, such as by evaporation or filtering, to obtain the dry, supported first catalyst component.
The first and second catalyst components may be contacted with the support in any order. In a particular exemplary embodiment of the invention, the first catalyst component is reacted first with the support as described above, then this supported first catalyst component is contacted with a second catalyst component.
Second Catalyst Component
As referred to herein, the term “second catalyst component” will be understood to refer to any catalyst component that is different from a first catalyst component. In an exemplary embodiment, the second catalyst component is a metallocene catalyst component.
Metallocene catalyst compounds are generally described throughout in 1 & 2 M
The Cp ligands are typically p-bonded and/or fused ring(s) or ring systems. The ring(s) or ring system(s) typically comprise atoms selected from the group consisting of Groups 13 to 16 atoms, and in a particular exemplary embodiment, the atoms that make up the Cp ligands are selected from the group consisting of carbon, nitrogen, oxygen, silicon, sulfur, phosphorous, germanium, boron and aluminum and combinations thereof, wherein carbon makes up at least 50% of the ring members. In a more particular exemplary embodiment, the Cp ligand(s) are selected from the group consisting of substituted and unsubstituted cyclopentadienyl ligands and ligands isolobal to cyclopentadienyl, non-limiting examples of which include cyclopentadienyl, indenyl, fluorenyl and other structures. Further non-limiting examples of such ligands include cyclopentadienyl, cyclopentaphenanthrenyl, indenyl, benzindenyl, fluorenyl, octahydrofluorenyl, cyclooctatetraenyl, cyclopentacyclododecene, phenanthrindenyl, 3,4-benzofluorenyl, 9-phenylfluorenyl, 8-H-cyclopent[a]acenaphthylenyl, 7H-dibenzofluorenyl, indeno[1,2-9]anthrene, thiophenoindenyl, thiophenofluorenyl, hydrogenated versions thereof (e.g., 4,5,6,7-tetrahydroindenyl, or “H4Ind”), substituted versions thereof, and heterocyclic versions thereof. In a particular exemplary embodiment, the metallocenes useful in the present invention are selected from those including one or two (two in a more particular exemplary embodiment) of the same or different Cp rings selected from the group consisting of cyclopentadienyl, indenyl, fluorenyl, tetrahydroindenyl, and substituted versions thereof.
The metal atom “M” of the metallocene catalyst compound may be selected from the group consisting of Groups 3 through 12 atoms and lanthanide Group atoms in one exemplary embodiment; and selected from the group consisting of Groups 3 through 10 atoms in a more particular exemplary embodiment; and selected from the group consisting of Sc, Ti, Zr, Hf, V, Nb, Ta, Mn, Re, Fe, Ru, Os, Co, Rh, Ir, and Ni in yet a more particular embodiment; and selected from the group consisting of Groups 4, 5 and 6 atoms in yet a more particular embodiment, and Ti, Zr, Hf atoms in yet a more particular embodiment, and Zr in still a more particular embodiment. The oxidation state of the metal atom “M” may range from 0 to +7 in one exemplary embodiment; and, in a more particular embodiment, may be +1, +2, +3, +4 or +5; and in yet a more particular embodiment may be +2, +3 or +4. The groups bound to the metal atom “M” are such that the compounds described below in the formulas and structures are electrically neutral, unless otherwise indicated. The Cp ligand(s) form at least one chemical bond with the metal atom M to form the “metallocene catalyst compound.” The Cp ligands are distinct from the leaving groups bound to the catalyst compound in that they are not highly susceptible to substitution/abstraction reactions.
In one exemplary embodiment, the supported bimetallic catalyst includes a metallocene catalyst component represented by the formula (I):
CpACpBMXn (I)
wherein M is as described above;
The ligands represented by CpA and CpB in formula (I) may be the same or different cyclopentadienyl ligands or ligands isolobal to cyclopentadienyl, either or both of which may contain heteroatoms, and either or both of which may be substituted by a group R. In one exemplary embodiment, CpA and CpB are independently selected from the group consisting of cyclopentadienyl, indenyl, tetrahydroindenyl, fluorenyl, and substituted derivatives of each.
Independently, each CpA and CpB of formula (I) may be unsubstituted or substituted with any one or combination of substituent groups R. Non-limiting examples of substituent groups R as used in structure (I) as well as ring substituents in structures (Va-d) include substituent groups R selected from the group consisting of hydrogen radicals, alkyls, alkenyls, alkynyls, cycloalkyls, aryls, acyls, aroyls, alkoxys, aryloxys, alkylthiols, dialkylamines, alkylamidos, alkoxycarbonyls, aryloxycarbonyls, carbomoyls, alkyl- and dialkyl-carbamoyls, acyloxys, acylaminos, aroylaminos, and combinations thereof. More particular non-limiting examples of alkyl substituent groups R associated with formulae (I) through (V) include methyl, ethyl, propyl, butyl, pentyl, hexyl, cyclopentyl, cyclohexyl, benzyl, phenyl, methylphenyl, and tert-butylphenyl groups and the like, including all their isomers, such as, for example, tertiary-butyl, isopropyl, and the like. Other possible radicals include substituted alkyls and aryls such as, for example, fluoromethyl, fluroethyl, difluroethyl, iodopropyl, bromohexyl, chlorobenzyl and hydrocarbyl substituted organometalloid radicals including trimethylsilyl, trimethylgermyl, methyldiethylsilyl and the like; and halocarbyl-substituted organometalloid radicals including tris(trifluoromethyl)silyl, methylbis(difluoromethyl)silyl, bromomethyldimethylgermyl and the like; and disubstituted boron radicals, including dimethylboron, for example; and disubstituted Group 15 radicals including dimethylamine, dimethylphosphine, diphenylamine, methylphenylphosphine; and Group 16 radicals including methoxy, ethoxy, propoxy, phenoxy, methylsulfide and ethylsulfide. Other substituent groups R include olefins such as, but not limited to, olefinically unsaturated substituents including vinyl-terminated ligands, for example 3-butenyl, 2-propenyl, 5-hexenyl and the like. In one exemplary embodiment, at least two R groups (two adjacent R groups in a particular exemplary embodiment) are joined to form a ring structure having from 3 to 30 atoms selected from the group consisting of carbon, nitrogen, oxygen, phosphorous, silicon, germanium, aluminum, boron and combinations thereof. Also, a substituent R group such as 1-butanyl may form a bonding association to the element M.
Each X in the formula (I) above, and for the formulae/structures (II) through (Va-d) below, is independently selected from the group consisting of: any leaving group, in one exemplary embodiment; halogen ions, hydrides, C1 to C12 alkyls, C2 to C12 alkenyls, C6 to C12 aryls, C7 to C20 alkylaryls, C1 to C12 alkoxys, C6 to C16 aryloxys, C7 to C18 alkylaryloxys, C1 to C12 fluoroalkyls, C6 to C12 fluoroaryls, and C1 to C12 heteroatom-containing hydrocarbons and substituted derivatives thereof in a more particular embodiment; hydride, halogen ions, C1 to C6 alkyls, C2 to C6 alkenyls, C7 to C18 alkylaryls, C1 to C6 alkoxys, C6 to C14 aryloxys, C7 to C16 alkylaryloxys, C1 to C6 alkylcarboxylates, C1 to C6 fluorinated alkylcarboxylates, C6 to C12 arylcarboxylates, C7 to C18 alkylarylcarboxylates, C1 to C6 fluoroalkyls, C2 to C6 fluoroalkenyls, and C7 to C18 fluoroalkylaryls in yet a more particular embodiment; hydride, chloride, fluoride, methyl, phenyl, phenoxy, benzoxy, tosyl, fluoromethyls and fluorophenyls in yet a more particular embodiment; C1 to C12 alkyls, C2 to C12 alkenyls, C6 to C12 aryls, C7 to C20 alkylaryls, substituted C1 to C12 alkyls, substituted C6 to C12 aryls, substituted C7 to C20 alkylaryls and C1 to C12 heteroatom-containing alkyls, C1 to C12 heteroatom-containing aryls and C1 to C12 heteroatom-containing alkylaryls in yet a more particular embodiment; chloride, fluoride, C1 to C6 alkyls, C2 to C6 alkenyls, C7 to C18 alkylaryls, halogenated C1 to C6 alkyls, halogenated C2 to C6 alkenyls, and halogenated C7 to C18 alkylaryls in yet a more particular embodiment; fluoride, methyl, ethyl, propyl, phenyl, methylphenyl, dimethylphenyl, trimethylphenyl, fluoromethyls (mono-, di- and trifluoromethyls) and fluorophenyls (mono-, di-, tri-, tetra- and pentafluorophenyls) in yet a more particular embodiment; and fluoride in yet a more particular embodiment.
Non-limiting examples of other X groups include alkyls, amines, phosphines, ethers, carboxylates, dienes, hydrocarbon radicals having from 1 to 20 carbon atoms; fluorinated hydrocarbon radicals (e.g., —C6F5 (pentafluorophenyl)), fluorinated alkylcarboxylates (e.g., CF3C(O)O−), hydrides and halogen ions and combinations thereof. Other examples of X ligands include alkyl groups such as cyclobutyl, cyclohexyl, methyl, heptyl, tolyl, trifluoromethyl, tetramethylene, pentamethylene, methylidene, methyoxy, ethyoxy, propoxy, phenoxy, bis(N-methylanilide), dimethylamide, dimethylphosphide radicals and the like. In one exemplary embodiment, two or more X's form a part of a fused ring or ring system.
In another exemplary embodiment, the supported bimetallic catalyst includes a metallocene catalyst component such as those of formula (I) where CpA and CpB are bridged to each other by at least one bridging group, (A), such that the structure is represented by formula (II):
CpA(A)CpBMXn (II)
These bridged compounds represented by formula (II) are known as “bridged metallocenes.” The elements CpA, CpB, M, X and n in structure (II) are as defined above for formula (I), each Cp ligand is chemically bonded to M, and (A) is chemically bonded to each Cp ligand. Non-limiting examples of bridging group (A) include divalent hydrocarbon groups containing at least one Group 13 to 16 atom, such as, but not limited to, at least one of a carbon, oxygen, nitrogen, silicon, aluminum, boron, germanium and tin atom, and combinations thereof, wherein the heteroatom may also be C1 to C12 alkyl- or aryl-substituted to satisfy neutral valency. The bridging group (A) may also contain substituent groups R as defined above (for formula (I)), including halogen radicals and iron. More particular non-limiting examples of bridging group (A) are represented by C1 to C6 alkylenes, substituted C1 to C6 alkylenes, oxygen, sulfur, R′2C—, R′2Si—, —Si(R′)2Si(R′2)—, R′2Ge—, R′P— (wherein “—” represents two chemical bonds), where R′ is independently selected from the group consisting of hydride, hydrocarbyl, substituted hydrocarbyl, halocarbyl, substituted halocarbyl, hydrocarbyl-substituted organometalloid, halocarbyl-substituted organometalloid, disubstituted boron, disubstituted Group 15 atoms, substituted Group 16 atoms, and halogen radical; and wherein two or more R′ may be joined to form a ring or ring system. In one exemplary embodiment, the bridged metallocene catalyst component of formula (II) has two or more bridging groups (A).
Other non-limiting examples of bridging group (A) include methylene, ethylene, ethylidene, propylidene, isopropylidene, diphenylmethylene, 1,2-dimethylethylene, 1,2-diphenylethylene, 1,1,2,2-tetramethylethylene, dimethylsilyl, diethylsilyl, methyl-ethylsilyl, trifluoromethylbutylsilyl, bis(trifluoromethyl)silyl, di(n-butyl)silyl, di(n-propyl)silyl, di(i-propyl)silyl, di(n-hexyl)silyl, dicyclohexylsilyl, diphenylsilyl, cyclohexylphenylsilyl, t-butylcyclohexylsilyl, di(t-butylphenyl)silyl, di(p-tolyl)silyl and the corresponding moieties wherein the Si atom is replaced by a Ge or a C atom; dimethylsilyl, diethylsilyl, dimethylgermyl and diethylgermyl.
In another exemplary embodiment, bridging group (A) may also be cyclic, comprising, for example, 4 to 10 ring members; in a more particular exemplary embodiment, bridging group (A) may comprise 5 to 7 ring members. The ring members may be selected from the elements mentioned above, and, in a particular exemplary embodiment, are selected from one or more of B, C, Si, Ge, N and O. Non-limiting examples of ring structures which may be present as, or as part of, the bridging moiety are cyclobutylidene, cyclopentylidene, cyclohexylidene, cycloheptylidene, cyclooctylidene and the corresponding rings where one or two carbon atoms are replaced by at least one of Si, Ge, N and O, in a particular exemplary embodiment, Si and Ge. The bonding arrangement between the ring and the Cp groups may be either cis-, trans-, or a combination.
The cyclic bridging groups (A) may be saturated or unsaturated and/or carry one or more substituents and/or be fused to one or more other ring structures. If present, the one or more substituents are, in one exemplary embodiment, selected from the group consisting of hydrocarbyl (e.g., alkyl such as methyl) and halogen (e.g., F, Cl). The one or more Cp groups to which the above cyclic bridging moieties may optionally be fused may be saturated or unsaturated, and are selected from the group consisting of those having 4 to 10 ring members, more particularly 5, 6 or 7 ring members (selected from the group consisting of C, N, O and S in a particular embodiment) such as, for example, cyclopentyl, cyclohexyl and phenyl. Moreover, these ring structures may themselves be fused such as, for example, in the case of a naphthyl group. Moreover, these (optionally fused) ring structures may carry one or more substituents. Illustrative, non-limiting examples of these substituents are hydrocarbyl (particularly alkyl) groups and halogen atoms.
The ligands CpA and CpB of formulae (I) and (II) are different from each other in one examplary embodiment, and the same in another exemplary embodiment.
In yet another exemplary embodiment, the supported bimetallic catalyst includes bridged mono-ligand metallocene compounds (e.g., mono cyclopentadienyl catalyst components). In this embodiment, the metallocene catalyst component is a bridged “half-sandwich” metallocene represented by the formula (III):
CpA(A)QMXr (III)
wherein CpA is defined above and is bound to M;
In formula (III), Q is a heteroatom-containing ligand in which the bonding atom (the atom that is bonded with the metal M) is, in one exemplary embodiment, selected from the group consisting of Group 15 atoms and Group 16 atoms. In yet a more particular embodiment, the bonding atom is selected from the group consisting of nitrogen, phosphorus, oxygen or sulfur atom. In still a more particular embodiment, the bonding atom is selected from the group consisting of nitrogen and oxygen. Non-limiting examples of Q groups include alkylamines, arylamines, mercapto compounds, ethoxy compounds, carboxylates (e.g., pivalate), carbamates, azenyl, azulene, pentalene, phosphoyl, phosphinimine, pyrrolyl, pyrozolyl, carbazolyl, borabenzene other compounds having Group 15 and Group 16 atoms capable of bonding with M.
In yet another exemplary embodiment, the supported bimetallic catalyst includes a component that is an unbridged “half sandwich” metallocene represented by the formula (IVa):
CpAMQqXw (IVa)
wherein CpA is defined as for the Cp groups in (I) and is a ligand that is bonded to M;
In formula (IVa), Q is selected from the group consisting of ROO−, RO—, R(O)—, —NR—, —CR2—, —S—, —NR2, —CR3, —SR, —SiR3, —PR2, —H, and substituted and unsubstituted aryl groups, R is selected from the group consisting of C1 to C6 alkyls, C6 to C12 aryls, C1 to C6 alkylamines, C6 to C12 alkylarylamines, C1 to C6 alkoxys, C6 to C12 aryloxys, and the like. Non-limiting examples of Q include C1 to C12 carbamates, C1 to C12 carboxylates (e.g., pivalate), C2 to C20 allyls, and C2 to C20 heteroallyl moieties.
Described another way, the “half sandwich” metallocenes above can be described as in formula (IVb), such as described in, for example, U.S. Pat. No. 6,069,213:
CpAM(W2GZ)Xy or
T(CpAM(W2GZ)Xy)
m (IVb)
wherein M, CpA, and X are as defined above;
In another aspect of the invention, the supported bimetallic catalyst includes a ene catalyst component that can be described more particularly in structures (Va), (Vb), (Vc) and (Vd):
The structure of the metallocene catalyst component represented by (Va) may take on many forms, such as those disclosed in, for example, U.S. Pat. No. 5,026,798, U.S. Pat. No. 5,703,187, and U.S. Pat. No. 5,747,406, including a dimer or oligomeric structure, such as disclosed in, for example, U.S. Pat. No. 5,026,798 and U.S. Pat. No. 6,069,213.
In a particular embodiment of the metallocene represented in (Vd), R1 and R2 form a conjugated 6-membered carbon ring system that may or may not be substituted.
Non-limiting examples of metallocene catalyst components consistent with the description herein include:
It is contemplated that the metallocene catalysts components described above include their structural or optical or enantiomeric isomers (racemic mixture), and, in one exemplary embodiment, may be a pure enantiomer.
As used herein, a single, bridged, asymmetrically substituted metallocene catalyst component having a racemic and/or meso isomer does not, itself, constitute at least two different bridged, metallocene catalyst components.
The “metallocene catalyst component” useful in the present invention may comprise any combination of any “embodiment” described herein.
When combined to form the bimetallic catalyst component, the molar ratio of metal from the first catalyst component to the second catalyst component (e.g., molar ratio of Ti:Zr) is a value of from 0.1:1 to 20:1 in one exemplary embodiment; and from 1:1 to 18:1 in another exemplary embodiment, and from 2:1 to 15:1 in yet another exemplary embodiment, and from 3:1 to 12:1 in yet another exemplary embodiment; and from 4:1 to 10:1 in yet another exemplary embodiment, and from 4:1 to 8:1 in yet another exemplary embodiment; wherein a desirable molar ratio of first catalyst component metal:second catalyst component metal is any combination of any upper limit with any lower limit described herein.
MAO-Activatable Compound
A “supported, treated catalyst system” comprises a bimetallic catalyst system that has been contacted with at least one compound that can be activated by methylalumoxane (“MAO-activatable compound”). Because the MAO-activatable compounds used with the present invention generally include transition metals, the supported, treated catalyst systems of the present invention generally have greater concentrations of transition metals (which can be activated by MAO) than do bimetallic catalyst systems. For example, in one embodiment, the supported, treated catalyst systems of the present invention have a transition metal concentration that is up to 25% greater than that of a typical bimetallic catalyst system; in another exemplary embodiment, the supported, treated catalyst systems of the present invention have a transition metal concentration that is more than 25% greater than that of a typical bimetallic catalyst system. Accordingly, the supported, treated catalyst systems of the present invention generally demonstrate more efficient use of MAO when they are used in polymerization processes than do typical bimetallic catalyst systems.
In an exemplary embodiment of the present invention, the at least one MAO-activatable compound is a metallocene catalyst compound, non-limiting examples of which have been previously described. In another exemplary embodiment, the at least one MAO-activatable compound is a Group-15-component-containing compound; a phenoxide catalyst compound; an additionally-discovered catalyst compound; or a conventional transition metal catalyst compound.
Group-15-Component-Containing Catalyst Compound
The at least one MAO-activatable compound may include one or more Group-15-component-containing catalyst compounds. The Group-15-component-containing compound generally includes a Group 3 to 14 metal atom, preferably a Group 3 to 7, more preferably a Group 4 to 6, and even more preferably a Group 4 metal atom, bound to at least one leaving group and also bound to at least two Group 15 atoms, at least one of which is also bound to a Group 15 or 16 atom through another group.
In one embodiment, at least one of the Group 15 atoms is also bound to a Group 15 or 16 atom through another group which may be a C1 to C20 hydrocarbon group, a heteroatom containing group, silicon, germanium, tin, lead, or phosphorus, wherein the Group 15 or 16 atom may also be bound to nothing or a hydrogen, a Group 14 atom containing group, a halogen, or a heteroatom containing group, and wherein each of the two Group 15 atoms are also bound to a cyclic group and may optionally be bound to hydrogen, a halogen, a heteroatom or a hydrocarbyl group, or a heteroatom containing group.
In another embodiment, the Group-15-component-containing compound of the present invention may be represented by the formulae:
The term “formal charge of the YZL or YZL′ ligand,” refers to the charge of the entire ligand absent the metal and the leaving groups X. The term “R1 and R2 may also be interconnected” means that R1 and R2 may be directly bound to each other or may be bound to each other through other groups. The term “R4 and R5 may also be interconnected” means that R4 and R5 may be directly bound to each other or may be bound to each other through other groups.
An alkyl group may be a linear, branched alkyl radicals, or alkenyl radicals, alkynyl radicals, cycloalkyl radicals or aryl radicals, acyl radicals, aroyl radicals, alkoxy radicals, aryloxy radicals, alkylthio radicals, dialkylamino radicals, alkoxycarbonyl radicals, aryloxycarbonyl radicals, carbomoyl radicals, alkyl- or dialkyl-carbamoyl radicals, acyloxy radicals, acylamino radicals, aroylamino radicals, straight, branched or cyclic, alkylene radicals, or combination thereof. An aralkyl group is defined to be a substituted aryl group.
In an exemplary embodiment, R4 and R5 are independently a group represented by the following formula:
wherein:
In a particular exemplary embodiment, R4 and R5 are both a group represented by the following formula:
In this embodiment, M is a Group 4 metal, preferably zirconium, titanium or hafnium, and even more preferably zirconium; each of L, Y, and Z is nitrogen; each of R1 and R2 is —CH2 —CH2—; R3 is hydrogen; and R6 and R7 are absent.
In a particular exemplary embodiment, the Group-15-component-containing compound is represented by Compound 1 below:
wherein “Ph” represents a phenyl group.
In exemplary embodiments of the present invention where the at least one MAO-activatable compound includes a Group-15-component-containing compound, the Group-15-component-containing compound may be prepared by methods known in the art, such as those disclosed in EP 0 893 454 A1, U.S. Pat. No. 5,889,128 and the references cited in U.S. Pat. No. 5,889,128. U.S. patent application Ser. No. 09/312,878, filed May 17, 1999, now U.S. Pat. No. 6,271,325, discloses a gas or slurry phase polymerization process using a supported bisamide catalyst.
A preferred direct synthesis of these compounds comprises reacting the neutral ligand, (see for example YZL or YZL′ of formula VI or VII) with MnXn (M is a Group 3 to 14 metal, n is the oxidation state of M, each X is an anionic group, such as halide), in a non-coordinating or weakly coordinating solvent, such as ether, toluene, xylene, benzene, methylene chloride, and/or hexane or other solvent having a boiling point above 60° C., at about 20 to about 150° C. (preferably 20 to 100° C.), preferably for 24 hours or more, then treating the mixture with an excess (such as four or more equivalents) of an alkylating agent, such as methyl magnesium bromide in ether. The magnesium salts are removed by filtration, and the metal complex isolated by standard techniques.
In one embodiment the Group-15-component-containing compound is prepared by a method comprising reacting a neutral ligand, (see for example YZL or YZL′ of formula VI or VII) with a compound represented by the formula MnXn (where M is a Group 3 to 14 metal, n is the oxidation state of M, each X is an anionic leaving group) in a non-coordinating or weakly coordinating solvent, at about 20° C. or above, preferably at about 20 to about 100° C., then treating the mixture with an excess of an alkylating agent, then recovering the metal complex. In a preferred embodiment the solvent has a boiling point above 60° C., such as toluene, xylene, benzene, and/or hexane. In another embodiment the solvent comprises ether and/or methylene chloride, either being preferable.
Additional information pertaining to Group-15-component-containing compounds may be found in, inter alia, EP 0 893 454 A1, which discloses transition metal amides combined with activators to polymerize olefins.
In one embodiment the Group-15-component-containing compound is allowed to age prior to use in a polymerization. It has been noted on at least one occasion that one such catalyst compound (aged at least 48 hours) performed better than a newly prepared catalyst compound.
Phenoxide Catalyst Compound
The at least one MAO-activatable compound may include one or more phenoxide catalyst compounds represented by the following formulae:
wherein R1 is hydrogen or a C4 to C100 group, preferably a tertiary alkyl group, preferably a C4 to C20 alkyl group, preferably a C4 to C20 tertiary alkyl group, preferably a neutral C4 to C100 group and may or may not also be bound to M, and at least one of R2 to R5 is a group containing a heteroatom, the rest of R2 to R5 are independently hydrogen or a C1 to C100 group, preferably a C4 to C20 alkyl group (preferably butyl, isobutyl, pentyl hexyl, heptyl, isohexyl, octyl, isooctyl, decyl, nonyl, dodecyl) and any of R2 to R5 also may or may not be bound to M, O is oxygen, M is a group 3 to group 10 transition metal or lanthanide metal, preferably a group 4 metal, preferably Ti, Zr or Hf, n is the valence state of the metal M, preferably 2, 3, 4, or 5, Q is an alkyl, halogen, benzyl, amide, carboxylate, carbamate, thiolate, hydride or alkoxide group, and may be bound to an R group containing a heteroatom, which may be any of R1 to R5. A heteroatom containing group may be any heteroatom or a heteroatom bound to carbon silica or another heteroatom. Preferred heteroatoms include boron, aluminum, silicon, nitrogen, phosphorus, arsenic, tin, lead, antimony, oxygen, selenium, tellurium. Particularly preferred heteroatoms include nitrogen, oxygen, phosphorus, and sulfur. Even more particularly preferred heteroatoms include oxygen and nitrogen. The heteroatom itself may be directly bound to the phenoxide ring or it may be bound to another atom or atoms that are bound to the phenoxide ring. The heteroatom containing group may contain one or more of the same or different heteroatoms. Preferred heteroatom groups include imines, amines, oxides, phosphines, ethers, ketenes, oxoazolines heterocyclics, oxazolines, thioethers, and the like. Particularly preferred heteroatom groups include imines. Any two adjacent R groups may form a ring structure, preferably a 5 or 6 membered ring. Likewise, the R groups may form multi-ring structures. In one embodiment any two or more R groups do not form a 5 membered ring.
In an exemplary embodiment, Q is bound to any of R2 to R5 and the R group to which Q is bound is a heteroatom-containing group.
This invention may also be practiced with the catalysts disclosed in EP 0 874 005 A1.
In an exemplary embodiment, the phenoxide catalyst compound includes one or more of:
The at least one MAO-activatable compound may include one or more complexes known as transition metal catalysts based on bidentate ligands containing pyridine or quinoline moieties, such as those described in U.S. patent application Ser. No. 09/103,620, filed Jun. 23, 1998 now U.S. Pat. No. 6,103,657.
In one embodiment, these catalyst compounds are represented by the formula:
((Z)XAt(YJ))qMQn Formula XII
where M is a metal selected from Group 3 to 13 or lanthanide and actinide series of the Periodic Table of Elements; Q is bonded to M and each Q is a monovalent, bivalent, or trivalent anion; X and Y are bonded to M; one or more of X and Y are heteroatoms, preferably both X and Y are heteroatoms; Y is contained in a heterocyclic ring J, where J comprises from 2 to 50 non-hydrogen atoms, preferably 2 to 30 carbon atoms; Z is bonded to X, where Z comprises 1 to 50 non-hydrogen atoms, preferably 1 to 50 carbon atoms, preferably Z is a cyclic group containing 3 to 50 atoms, preferably 3 to 30 carbon atoms; t is 0 or 1; when t is 1, A is a bridging group joined to at least one of X, Y or J, preferably X and J; q is 1 or 2; n is an integer from 1 to 4 depending on the oxidation state of M. In one embodiment, where X is oxygen or sulfur then Z is optional. In another embodiment, where X is nitrogen or phosphorous then Z is present. In an embodiment, Z is preferably an aryl group, more preferably a substituted aryl group.
In one exemplary embodiment, the catalyst compounds include complexes of Ni2+ and Pd2+ described in the articles Johnson, et al., “New Pd(II)— and Ni(II)— Based Catalysts for Polymerization of Ethylene and a-Olefins,” J. Am. Chem. Soc. 1995, 117, 6414-6415 and Johnson et al., “Copolymerization of Ethylene and Propylene with Functionalized Vinyl Monomers by Palladium(II) Catalysts,” J. Am. Chem. Soc., 1996, 118, 267-268, and WO 96/23010 published Aug. 1, 1996, WO 99/02472, U.S. Pat. Nos. 5,852,145, 5,866,663 and 5,880,241. These complexes can be either dialkyl ether adducts, or alkylated reaction products of the described dihalide complexes that can be activated to a cationic state by the activators of this invention described below.
Other catalyst compounds include