WO2001030864A2 - Polymeres nanocomposites - Google Patents
Polymeres nanocomposites Download PDFInfo
- Publication number
- WO2001030864A2 WO2001030864A2 PCT/US2000/027840 US0027840W WO0130864A2 WO 2001030864 A2 WO2001030864 A2 WO 2001030864A2 US 0027840 W US0027840 W US 0027840W WO 0130864 A2 WO0130864 A2 WO 0130864A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- composition
- layered silicate
- acid
- cation exchanging
- acid treated
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2282—Unsaturated compounds used as ligands
- B01J31/2291—Olefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/08—Silica
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/16—Clays or other mineral silicates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/049—Pillared clays
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/12—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides
- B01J31/14—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
- B01J31/143—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron of aluminium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/1616—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2282—Unsaturated compounds used as ligands
- B01J31/2295—Cyclic compounds, e.g. cyclopentadienyls
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/152—Preparation of hydrogels
- C01B33/154—Preparation of hydrogels by acidic treatment of aqueous silicate solutions
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/157—After-treatment of gels
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/02—Carriers therefor
- C08F4/025—Metal oxides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K9/00—Use of pretreated ingredients
- C08K9/08—Ingredients agglomerated by treatment with a binding agent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
- B01J2531/48—Zirconium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
- B01J2531/49—Hafnium
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65908—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/6592—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/6592—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
- C08F4/65922—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not
- C08F4/65927—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not two cyclopentadienyl rings being mutually bridged
Definitions
- the instant invention relates to nanocomposite polymers.
- European Patent Application publication number EP 0 747 322 Al describes nanocomposite polymers made by blending quaternary ammonium treated cation exchanging layered silicate materials with a polar group modified polymer.
- Such nanocomposite polymers exhibit improved properties such as increased tensile modulus relative to the base polymer.
- the degree of improvement in the properties of such nanocomposite polymers is not as great as desired. It would be an advance in the art of nanocomposite polymers if the degree of improvement were greater. For example, it would be a clear advance in the art if a polypropylene nanocomposite were developed which had a tensile modulus of more than four hundred thousand pounds per square inch using ten percent or less filler.
- the instant invention is a solution to the above mentioned problem to a large degree.
- using the instant invention it is possible to prepare a polypropylene nanocomposite having a tensile modulus of more than four hundred thousand pounds per square inch using ten percent or less filler.
- the instant invention is a method for producing a nanocomposite polymer, comprising the step of adding an olefin to a metallocene polymerization catalyst treated dispersion of an acid treated cation exchanging layered silicate material in a solvent so that the olefin polymerizes to form the nanocomposite polymer.
- the instant invention is a composition of matter comprising an exfoliated acid treated cation exchanging layered silicate material dispersed in a polymer matrix, wherein more than about fifty percent of the acid treated cation exchanging layered silicate material is found by electron microscopy to have five or fewer layers.
- the instant invention is a composition of matter, comprising a metallocene polymerization catalyst treated, acid treated cation exchanging layered silicate material.
- Fig. 1 is a drawing reproduction of a photomicrograph of a nanocomposite polymer of the instant invention.
- the invention is a method for producing a nanocomposite polymer.
- a nanocomposite polymer is by definition herein a polymer having dispersed therein sufficiently exfoliated cation exchanging layered silicate material.
- the term "sufficiently exfoliated” means that more than about twenty five percent by weight of the acid treated layered silicate material is found by electron microscopy of the nanocomposite polymer to have five or fewer layers.
- the thickness of a single layer of such material is one to two nanometers while the length and width of such layer can be in the range of, for example, one hundred to one thousand nanometers.
- Photomicrographs of nanocomposite polymers typically show a dispersion of multiple layer units of the multi-layered silicate material in the polymer, such as, two, three, four, five and more than five layer units dispersed in the polymer. It is generally desired to achieve a high degree of exfoliation of the multi-layered silicate material. Ideally the degree of such exfoliation is so extensive that only single layer units are present.
- FIG. 1 therein is shown a drawing reproduction of an idealized representative photomicrograph of a nanocomposite polymer of the instant invention.
- Fig. 1 shows two one layer units and one each of a two, three, four, five, six and seven layer unit.
- the nanocomposite polymer shown in Fig. 1 has about 55 percent five or fewer layer units on a weight percent basis since each of the layers are essentially the same size.
- Examples of cation exchanging layered silicate materials include: 1) biophilite, kaolinite, dickalite or talc clays, 2) smectite clays, 3) vermiculite clays,
- Zeolitic layered materials such as ITQ-2, MCM-22 precursor, exfoliated ferrierite and exfoliated mordenite.
- clay materials exist in nature, and also can be synthesized, generally in higher purity than the native material. Any of the naturally occurring or synthetic cation exchanging layered silicate clay materials may be used in the present invention. Preferred are smectite clays, including montmorillonite, bidelite, saponite and hectorite.
- cation exchanging layered silicate material also includes the “layered fiber” silicate materials such as attapulgite and sepiolite.
- Layered fiber silicate materials exfoliate to produce multi-fiber units (herein multi-layer units) and most preferably they exfoliate to produce single fiber units (herein single layer units) dispersed in the polymer.
- the cation exchanging layered silicate material is acidified by contacting it with a Bronsted acid (such as, hydrochloric acid, sulfuric acid, a carboxylic acid, an amino acid or any material which forms an acidic aqueous dispersion such as acidic metal salts like zinc sulfate) or by contacting it with an acidified amine (such as, an amine hydrochloride such as 4-tetradecyl aniline hydrochloride).
- a Bronsted acid such as, hydrochloric acid, sulfuric acid, a carboxylic acid, an amino acid or any material which forms an acidic aqueous dispersion such as acidic metal salts like zinc sulfate
- an acidified amine such as, an amine hydrochloride such as 4-tetradecyl aniline hydrochloride.
- a Bronsted acid such as, hydrochloric acid, sulfuric acid, a carboxylic acid, an amino acid or any material which forms an acidic aqueous dis
- the acidified layered silicate material is dispersed with a solvent (such as, toluene). Most preferably, such dispersion is accomplished by sonication. However, such dispersions can also be made by any suitable technique such as high shear mixing or wet ball milling.
- the dispersion may then contacted with a metallocene polymerization catalyst to produce a metallocene treated sonicated dispersion.
- Metallocene polymerization catalysts are well known in the art and include derivatives of Group 3, 4, or Lanthanide metals which are in the +2, +3, or +4 formal oxidation state.
- Preferred compounds include metal complexes containing from 1 to 3 ⁇ -bonded anionic or neutral ligand groups, which may be cyclic or non-cyclic delocalized ⁇ -bonded anionic ligand groups.
- ⁇ -bonded anionic ligand groups are conjugated or nonconjugated, cyclic or non-cyclic dienyl groups, allyl groups, boratabenzene groups, and arene groups.
- ⁇ -bonded is meant that the ligand group is bonded to the transition metal by a sharing or donating of electrons from a partially delocalized ⁇ -bond.
- Each atom in the delocalized ⁇ -bonded group may independently be substituted with a radical selected from the group consisting of hydrogen, halogen, hydrocarbyl, halohydrocarbyl, hydrocarbyl-substituted metalloid radicals wherein the metalloid is selected from Group 14 of the Periodic Table of the Elements, and such hydrocarbyl- or hydrocarbyl-substituted metalloid radicals further substituted with a Group 15 or 16 hetero atom containing moiety.
- hydrocarbyl C ⁇ _20 straight, branched and cyclic alkyl radicals, C6_20 aromatic radicals, C7.20 alkyl-substituted aromatic radicals, and C7.20 aryl-substituted alkyl radicals.
- two or more such radicals may together form a fused ring system, including partially or fully hydrogenated fused ring systems, or they may form a metallocycle with the metal.
- Suitable hydrocarbyl- substituted organometalloid radicals include mono-, di- and tri-substituted organometalloid radicals of Group 14 elements wherein each of the hydrocarbyl groups contains from 1 to 20 carbon atoms.
- hydrocarbyl-substituted organometalloid radicals include trimethylsilyl, triethylsilyl, ethyldimethylsilyl, methyldiethylsilyl, triphenylgermyl, and trimethylgermyl groups.
- Group 15 or 16 hetero atom containing moieties include amine, phosphine, ether or thioether moieties or divalent derivatives thereof, e. g., amide, phosphide, ether or thioether groups bonded to the transition metal or Lanthanide metal, and bonded to the hydrocarbyl group or to the hydrocarbyl- substituted metalloid containing group.
- Suitable anionic, delocalized ⁇ -bonded groups include cyclopentadienyl, indenyl, fluorenyl, tetrahydroindenyl, tetrahydrofluorenyl, octahydrofluorenyl, pentadienyl, cyclohexadienyl, dihydroanthracenyl, hexahydroanthracenyl, decahydroanthracenyl groups, and boratabenzene groups, as well as Cj-io hydrocarbyl-substituted or C 1-10 hydrocarbyl-substituted silyl substituted derivatives thereof.
- Preferred anionic delocalized ⁇ -bonded groups are cyclopentadienyl, pentamethylcyclopentadienyl, tetramethylcyclopentadienyl, tetramethylsilylcyclo- pentadienyl, indenyl, 2,3-dimethylindenyl, fluorenyl, 2-methylindenyl, 2-methyl-4- phenylindenyl, tetrahydrofluorenyl, octahydrofluorenyl, and tetrahydroindenyl.
- boratabenzenes are anionic ligands which are boron containing analogues to benzene. They are previously known in the art having been described by G. Herberich. et al maneuver in Organometallics. 14,1, 471-480 (1995). Preferred boratabenzenes correspond to the formula:
- R" is selected from the group consisting of hydrocarbyl, silyl, or germyl, said R" having up to 20 non-hydrogen atoms.
- R" is selected from the group consisting of hydrocarbyl, silyl, or germyl, said R" having up to 20 non-hydrogen atoms.
- a suitable class of catalysts are transition metal complexes corresponding to the formula: K' j MZ'mLiXp, or a dimer thereof
- K' is an anionic group containing delocalized ⁇ -electrons through which K' is bound to M, said K' group containing up to 50 atoms not counting hydrogen atoms, optionally two K' groups may be joined together forming a bridged structure, and further optionally one K' may be bound to Z' ;
- M is a metal of Group 4 of the Periodic Table of the Elements in the +2, +3 or +4 formal oxidation state;
- Z' is an optional, divalent substituent of up to 50 non-hydrogen atoms that together with K forms a metallocycle with M;
- L is an optional neutral ligand having up to 20 non-hydrogen atoms;
- X each occurrence is a monovalent, anionic moiety having up to 40 non- hydrogen atoms
- two X groups may be covalently bound together forming a divalent dianionic moiety having both valences bound to M
- 2 X groups may be covalently bound together to form a neutral, conjugated or nonconjugated diene that is bound to M by means of delocalized ⁇ -electrons (whereupon M is in the +2 oxidation state), or further optionally one or more X and one or more L groups may be bonded together thereby forming a moiety that is both covalently bound to M and coordinated thereto by means of Lewis base functionality
- k is 0, 1 or 2
- m is 0 or 1;
- 1 is a number from 0 to 3; p is an integer from 0 to 3; and the sum, k+m+p, is equal to the formal oxidation state of M, except when 2 X groups together form a neutral conjugated or non-conjugated diene that is bound to M via delocalized ⁇ -electrons, in which case the sum k+m is equal to the formal oxidation state of M.
- Preferred complexes include those containing either one or two K' groups.
- the latter complexes include those containing a bridging group linking the two K' groups.
- Preferred bridging groups are those corresponding to the formula (ER'2) X wherein E is silicon, germanium, tin, or carbon, R' independently each occurrence is hydrogen or a group selected from silyl, hydrocarbyl, hydrocarbyloxy and combinations thereof, said R' having up to 30 carbon or silicon atoms, and x is 1 to 8.
- R' independently each occurrence is methyl, ethyl, propyl, benzyl, tert-butyl, phenyl, methoxy, ethoxy or phenoxy.
- Examples of the complexes containing two K' groups are compounds corresponding to the formula:
- M is titanium, zirconium or hafnium, preferably zirconium or hafnium, in the
- R in each occurrence independently is selected from the group consisting of hydrogen, hydrocarbyl, silyl, germyl, cyano, halo and combinations thereof, said R 3 having up to 20 non-hydrogen atoms, or adjacent R 3 groups together form a divalent derivative (for example, a hydrocarbadiyl, siladiyl or germadiyl group) thereby forming a fused ring system, and
- X independently each occurrence is an anionic ligand group of up to 40 non- hydrogen atoms, or two X" groups together form a divalent anionic ligand group of up to 40 non-hydrogen atoms or together are a conjugated diene having from 4 to 30 non-hydrogen atoms bound by means of delocalized ⁇ -electrons to M, whereupon M is in the +2 formal oxidation state, and
- R', E and x are as previously defined.
- the foregoing metal complexes are especially suited for the preparation of polymers having stereoregular molecular structure. In such capacity it is preferred that the complex possesses C s or C 2 symmetry or possesses a chiral, stereorigid structure.
- Examples of the first type are compounds possessing different delocalized ⁇ -bonded ligand groups, such as one cyclopentadienyl group and one fluorenyl group. Similar systems based on Ti(IV) or Zr(IV) were disclosed for preparation of syndiotactic olefin polymers in Ewen, et al., J. Am. Chem. Soc. 1 10, 6255-6256 (1980).
- Examples of chiral structures include rac WO 01/30864 PCT/TJSOO/27840 bis-indenyl complexes. Similar systems based on Ti(IV) or Zr(IV) were disclosed for preparation of isotactic olefin polymers in Wild et al., J. Organomet. Chem.. 232, 233-47, (1982).
- Exemplary bridged ligands containing two ⁇ -bonded groups are: 5 dimethylbis(cyclopentadienyl)silane, dimethylbis(tetramethylcyclopentadienyl)silane, dimethylbis(2-ethylcyclopentadien-l-yl)silane, dimethylbis(2-t-butylcyclopentadien-l- yl)silane, 2,2-bis(tetramethylcyclopentadienyl)propane, dimethylbis(inden- 1 -yl)silane, dimethylbis(tetrahydroinden- 1 -yl)silane, dimethylbis(fluoren- 1 -yl)silane, dimethylbis(tetrahydrofluoren- 1 -yl)silane, dimethylbis(2-methyl-4-phenylinden- 1 -yl)-silane, o dimethylbis(2-methylinden- 1 -yl)silane
- Preferred X" groups are selected from hydride, hydrocarbyl, silyl, germyl, halohydrocarbyl, halosilyl, silylhydrocarbyl and aminohydrocarbyl groups, or two X" groups together form a divalent derivative of a conjugated diene or else together they form a neutral, ⁇ -bonded, conjugated diene. Most preferred X" groups are C ⁇ _20 hydrocarbyl groups. 0
- a further class of metal complexes utilized in the present invention corresponds to the preceding formula or a dimer thereof, wherein Z' is a divalent substituent of up to 50 non-hydrogen atoms that together with K' forms a metallocycle with M.
- Preferred divalent Z' substituents include groups containing up to 30 non- 5 hydrogen atoms comprising at least one atom that is oxygen, sulfur, boron or a member of
- a preferred class of such Group 4 metal coordination complexes used o according to the present invention corresponds to the formula:
- M is titanium or zirconium, preferably titanium in the +2, +3, or +4 formal oxidation state;
- R in each occurrence independently is selected from the group consisting of hydrogen, hydrocarbyl, silyl, germyl, cyano, halo and combinations thereof, said R 3 having up to 20 non-hydrogen atoms, or adjacent R 3 groups together form a divalent derivative (for example, a hydrocarbadiyl, siladiyl or germadiyl group) thereby forming a fused ring system
- each X is a halo, hydrocarbyl, hydrocarbyloxy or silyl group, said group having up to 20 non-hydrogen atoms, or two X groups together form a neutral C5.30 conjugated diene or a divalent derivative thereof;
- Y is -O-, -S-, -NR'-, -PR'-; and
- Illustrative Group 4 metal complexes that may be employed in the practice of the present invention include: cyclopentadienyltitaniumtrimethyl, cyclopentadienyltitaniumtriethyl, cyclopentadienyltitaniumtriisopropyl, cyclopentadienyltitaniumtriphenyl, cyclopentadienyltitaniumtribenzyl, cyclopentadienyltitanium-2,4-dimethylpentadienyl, cyclopentadienyltitanium-2,4-dimethylpentadienyl»triethylphosphine, WO 01/30864 PCT/TJSOO/27840 cyclopentadienyltitanium-2,4-dimethylpentadienyl»trimethylphosphine, cyclopentadienyltitaniumdimethylmethoxide, cyclopen
- Complexes containing two K' groups including bridged complexes suitable for use in the present invention include: bis(cyclopentadienyl)zirconiumdimethyl, bis(cyclopentadienyl)zirconium dibenzyl, bis(cyclopentadienyl)zirconium methyl benzyl, bis(cyclopentadienyl)zirconium methyl phenyl, bis(cyclopentadienyl)zirconiumdiphenyl, bis(cyclopentadienyl)titanium-allyl, bis(cyclopentadienyl)zirconiummethylmethoxide, bis(cyclopentadienyl)zirconiummethylchloride, bis(pentamethylcyclopentadienyl)zirconiumdimethyl, bis(pentamethylcyclopentadienyl)titaniumdimethyl, bis(indenyl)zirconiumdimethyl, indenylfluor
- metallocene polymerization catalysts including Ziegler-Natta catalysts and Brookhart/Gibson catalysts
- the metallocene polymerization catalyst can alternatively be added during the dispersion of the layered silicate material.
- the relative amount of metallocene polymerization catalyst is the same in the instant invention as in the prior art of metallocene catalysts and depends on the specific catalyst used. It should be 0 understood that the instant invention may be used for any polymerization process including solution, slurry and gas phase polymerization and that any polymerization catalyst may be used that is acid activated.
- the olefin 5 polymerizes to form the nanocomposite polymer. It is believed that the acid component of the acidified layered silicate material activates the metallocene polymerization catalyst to produce polymer between the layers of the layered silicate material and thereby separate or exfoliate such layers to a greater degree into the developing polymer matrix. In addition, it is believed that the temperature of the polymerization should be sufficiently low so that o more of the polymerization occurs between the layers of the layered silicate in order to promote a greater degree of such exfoliation.
- the residual hydroxyl or other reactive functionality of the acid treated cation exchanging layered silicate material is capped or reacted with a reactive 5 material, especially a Lewis acid.
- a reactive 5 material especially a Lewis acid.
- Preferred Lewis acids include trialkyl aluminum compounds having from 1 to 10 carbons in each alkyl group.
- metallocene polymerization catalyst treated, acid treated cation exchanging layered silicate material means a cation exchanging layered silicate material that has been contacted with an acid and a metallocene polymerization catalyst as discussed o above. It should be understood that a metallocene polymerization catalyst treated, acid treated cation exchanging layered silicate material may be used in a solution, slurry or gas phase polymerization system.
- the resulting nanocomposite polymer preferably comprises an exfoliated acid treated cation exchanging layered silicate material dispersed in a polymer matrix, wherein more than about fifty percent by weight of the acid treated layered silicate material is found by electron microscopy of the nanocomposite polymer to have five or fewer layers.
- the weight percent of acid treated cation exchanging layered silicate material in the nanocomposite polymer is more than one percent and less than ten percent.
- Such nanocomposite polymers are capable of unexpected tensile modulus, such as, more than four hundred thousand pounds per square inch. With specific regard to polypropylene nanocomposites, unexpected tensile modulus of more than five hundred thousand pounds per square inch are described below.
- the standard test method for determining tensile modulus herein is ASTM Method Number D882.
- the olefin used in the instant invention is selected from the group of olefins having from two to ten carbon atoms.
- olefins include, for example, styrene, divinylbenzene, norborene, ethylene, propylene, octene, butadiene and mixtures thereof.
- the polymer product of or by way of the instant invention may be, for example, a rubber, a thermoplastic elastomer, polyethylene and polypropylene.
- One half gram of vacuum dried 4-tetradecylanilinium exchanged montmorillonite is added to one hundred and twenty milliliters of dry toluene to produce a slurry.
- Six hundred microliters of tripropylaluminum is added to the slurry.
- Five hundred microliters of a two and one half millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2-methyl-4-phenylindenys) zirconium (II) l,4-diphenyl-l,3-butadiene) is added to the slurry.
- the slurry is then sonicated for fifteen minutes.
- the sonicated slurry is then aged for one hour.
- Example 1 is repeated except that the polymerization reaction is one half hour at room temperature followed by one half hour at eighty degrees Celcius. Seven grams of polypropylene nanocomposite is recovered by acetone precipitation. The polymer has a number average molecular weight of 17,100. Electron microscopy of the polymer shows substantial single layer exfoliation of the montmorillonite but to a somewhat lesser degree than the polymer of Example 1.
- Example 1 is repeated except that one-quarter gram of treated montmorillonite is used and the polymerization reaction is one hour at eighty degrees Celcius. Seven grams of polypropylene nanocomposite is recovered by acetone precipitation. The polymer has a number average molecular weight of 6,200. Electron microscopy of the polymer shows substantial single layer exfoliation of the montmorillonite but to a somewhat lesser degree than the polymer of Example 2.
- Example 1 is repeated except that one-quarter gram of treated montmorillonite is used and the polymerization reaction is three quarters of one hour at room temperature. Seven grams of polypropylene nanocomposite is recovered by acetone precipitation. The polymer has a number average molecular weight of 103,000. Electron microscopy of the polymer shows substantial single layer exfoliation of the montmorillonite to about the same degree than the polymer of Example 1.
- Example 1 is repeated except that one-quarter gram of treated montmorillonite is used and the polymerization reaction is one quarter of one hour at eighty- five degrees Celcius. Ten grams of polypropylene nanocomposite is recovered by acetone precipitation. The polymer has a number average molecular weight of 18,700. Electron microscopy of the polymer shows some single layer exfoliation of the montmorillonite but less than that of Example 3.
- Two grams of vacuum dried 4-tetradecylanilinium exchanged montmorillonite is added to four hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of tripropylaluminum is added to the slurry.
- Five hundred microliters of a two and one half millimolar solution of metallocene polymerization catalyst (dimethylsilyl- bis(2-methyl-4-phenylindenys) zirconium (II) l ,4-diphenyl-l ,3-butadiene) is added to the slurry.
- the slurry is then sonicated for thirty minutes.
- the sonicated slurry is then aged for sixteen hours.
- Example 6 is repeated except that the polymerization reaction is carried out for fifteen minutes. Fifteen grams of the resulting polypropylene nanocomposite is recovered. The tensile modulus of the resulting polypropylene nanocomposite is four hundred and eighty three thousand pounds per square inch. Electron microscopy examination of the resulting polypropylene nanocomposite shows substantial single layer exfoliation of the montmorillonite but to a somewhat lesser degree than that of Example 6.
- Two grams of vacuum dried 4-tetradecylanilinium exchanged fluoromica is added to four hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of one molar tripropylaluminum in toluene is added to the slurry.
- One milliliter of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2- methyl-4-phenylindenys) zirconium (II) 1,4-diphenyl- 1,3 -butadiene) is added to the slurry.
- the slurry is then sonicated for thirty minutes.
- the sonicated slurry is then aged for five hours.
- Two grams of vacuum dried 4-tetradecylanilinium exchanged fluoromica is added to four hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of one molar tripropylaluminum in toluene is added to the slurry.
- One milliliter of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2- methyl-4-phenylindenys) zirconium (H) 1,4-diphenyl- 1,3 -butadiene) is added to the slurry.
- the slurry is then sonicated for thirty minutes.
- the sonicated slurry is then aged for one day.
- propylene gas at twenty pounds per square inch is contacted with the slurry for thirty minutes at room temperature.
- Twenty five grams of polypropylene nanocomposite is recovered by acetone precipitation.
- the polymer has a number average molecular weight of 170,000.
- the tensile modulus of the polypropylene nanocomposite is 434,000 pounds per square inch (psi).
- Example 9 The experiment of Example 9 is repeated six times using the polymerization times noted below. Pol. Time Molecular Wt. Tensile Mod. Pol. Wt.
- Two grams of vacuum dried 4-tetradecylanilinium exchanged montmorillonite is added to four hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of one molar tripropylaluminum in toluene is added to the slurry.
- One milliliter of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2- methyl-4-phenylindenys) zirconium (II) 1,4-diphenyl- 1 ,3-butadiene) is added to the slurry.
- the slurry is then sonicated for twenty minutes.
- the sonicated slurry is then aged for one hour.
- propylene gas at twenty pounds per square inch is contacted with the slurry for thirty minutes at room temperature.
- Twenty grams of polypropylene nanocomposite is recovered by acetone precipitation.
- the polymer has a number average molecular weight of 303,000.
- the tensile modulus of the polypropylene nanocomposite is 522,000 pounds per square inch (psi).
- Example 11 The experiment of Example 11 is repeated five times with the following results. Molecular Wt. Tensile Mod. Pol. Wt.
- One gram of vacuum dried anilinium exchanged montmorillonite is added to one hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of one molar tripropylaluminum in toluene is added to the slurry.
- One milliliter of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2-methyl-4- phenylindenys) zirconium (ET) 1,4-diphenyl- 1,3 -butadiene) is added to the slurry.
- the slurry is then sonicated for thirty minutes.
- the sonicated slurry is then aged for one hour.
- propylene gas at twenty pounds per square inch is contacted with the slurry at the temperatures shown below with the following results.
- One gram of vacuum dried anilinium exchanged montmorillonite is added to one hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of one molar tripropylaluminum in toluene is added to the slurry.
- Two milliliters of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2-methyl-4- phenylindenys) zirconium (II) 1,4-diphenyl- 1,3-butadiene) is added to the slurry.
- the slurry is then sonicated for thirty minutes.
- the sonicated slurry is then aged for one hour.
- propylene gas at twenty pounds per square inch is contacted with the slurry at the temperatures shown below with the following results.
- One gram of freeze dried hydrochloric acid treated attapulgite is added to four hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of one molar tripropylaluminum in toluene is added to the slurry.
- One milliliter of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2-methyl-4- phenylindenys) zirconium (II) 1,4-diphenyl- 1,3-butadiene) is added to the slurry.
- the slurry is then sonicated for thirty minutes.
- the sonicated slurry is then aged for one hour.
- propylene gas at twenty pounds per square inch is contacted with the slurry at the temperatures shown below with the following results.
- One gram of freeze dried hydrochloric acid treated attapulgite is added to four hundred milliliters of dry toluene to produce a slurry.
- Five milliliters of one molar tripropylaluminum in toluene is added to the slurry.
- Two milliliters of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2-methyl-4- phenylindenys) zirconium (II) 1,4-diphenyl- 1,3-butadiene) is added to the slurry.
- the slurry is then sonicated for thirty minutes.
- the sonicated slurry is then aged for one hour.
- propylene gas at twenty pounds per square inch is contacted with the slurry at the temperatures shown below with the following results.
- tetradecylanalinium treated fluoromica Two grams of tetradecylanalinium treated fluoromica is added to four hundred milliliters of dry toluene to produce a slurry. Five milliliters of one molar tripropylaluminum in toluene is added to the slurry. One milliliter of a one and one quarter millimolar solution of metallocene polymerization catalyst (dimethylsilyl-bis(2-methyl-4- phenylindenys) zirconium (II) 1,4-diphenyl- 1,3-butadiene) is added to the slurry. The slurry is then sonicated for thirty minutes. The sonicated slurry is then aged for one day. Then, ethylene gas at ten pounds per square inch is contacted with the slurry at the temperatures shown below with the following results.
- metallocene polymerization catalyst dimethylsilyl-bis(2-methyl-4- phenylindeny
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Polymers & Plastics (AREA)
- Medicinal Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Polymerisation Methods In General (AREA)
- Silicon Compounds (AREA)
- Catalysts (AREA)
Abstract
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU34340/01A AU3434001A (en) | 1999-10-07 | 2000-10-06 | Nanocomposite polymers |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15807299P | 1999-10-07 | 1999-10-07 | |
US60/158,072 | 1999-10-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2001030864A2 true WO2001030864A2 (fr) | 2001-05-03 |
WO2001030864A3 WO2001030864A3 (fr) | 2002-03-28 |
Family
ID=22566578
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2000/027839 WO2001025149A2 (fr) | 1999-10-07 | 2000-10-06 | Composition de gel de silice et procede de fabrication |
PCT/US2000/027840 WO2001030864A2 (fr) | 1999-10-07 | 2000-10-06 | Polymeres nanocomposites |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2000/027839 WO2001025149A2 (fr) | 1999-10-07 | 2000-10-06 | Composition de gel de silice et procede de fabrication |
Country Status (2)
Country | Link |
---|---|
AU (2) | AU1330701A (fr) |
WO (2) | WO2001025149A2 (fr) |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6583209B2 (en) | 2001-09-06 | 2003-06-24 | Equistar Chemicals, Lp | Propylene polymer composites having improved melt strength |
US6646072B2 (en) | 2002-01-23 | 2003-11-11 | Equistar Chemicals, Lp | Process for making polyolefin compositions containing exfoliated clay |
US6770697B2 (en) | 2001-02-20 | 2004-08-03 | Solvay Engineered Polymers | High melt-strength polyolefin composites and methods for making and using same |
US6884834B2 (en) | 2002-09-19 | 2005-04-26 | Equistar Chemicals, Lp | Shear modification of HDPE-clay nanocomposites |
US6942120B2 (en) | 2002-06-07 | 2005-09-13 | S.C. Johnson & Son, Inc. | Disposable bakeware with improved drip resistance at elevated temperatures |
US7037970B2 (en) | 2001-12-20 | 2006-05-02 | Equistar Chemicals, Lp | Process for increasing the melt strength of ethylene-vinyl carboxylate copolymers |
US7220695B2 (en) | 2004-01-07 | 2007-05-22 | Exxonmobil Chemical Patents Inc. | Supported activator |
WO2007146263A3 (fr) * | 2006-06-12 | 2008-02-14 | Univ California | Procédé servant à former des nanocomposites d'argile exfoliée-polyoléfine |
US7432319B2 (en) | 2005-11-29 | 2008-10-07 | Honglan Lu | Process for making exfoliated polyolefin/clay nanocomposites |
US7517353B2 (en) | 2001-09-28 | 2009-04-14 | Boston Scientific Scimed, Inc. | Medical devices comprising nanomaterials and therapeutic methods utilizing the same |
US7754789B1 (en) | 2006-06-12 | 2010-07-13 | The Regents Of The University Of California | Method for forming flame-retardant clay-polyolefin composites |
US9283704B2 (en) | 2001-06-18 | 2016-03-15 | Becton, Dickinson And Company | Multilayer containers |
US9321854B2 (en) | 2013-10-29 | 2016-04-26 | Exxonmobil Chemical Patents Inc. | Aluminum alkyl with C5 cyclic and pendent olefin polymerization catalyst |
US10059788B2 (en) | 2016-04-29 | 2018-08-28 | Exxonmobil Chemical Patents Inc. | Organoaluminum activators on clays |
US10562987B2 (en) | 2016-06-30 | 2020-02-18 | Exxonmobil Chemical Patents Inc. | Polymers produced via use of quinolinyldiamido transition metal complexes and vinyl transfer agents |
US10618988B2 (en) | 2015-08-31 | 2020-04-14 | Exxonmobil Chemical Patents Inc. | Branched propylene polymers produced via use of vinyl transfer agents and processes for production thereof |
US10626200B2 (en) | 2017-02-28 | 2020-04-21 | Exxonmobil Chemical Patents Inc. | Branched EPDM polymers produced via use of vinyl transfer agents and processes for production thereof |
US10676551B2 (en) | 2017-03-01 | 2020-06-09 | Exxonmobil Chemical Patents Inc. | Branched ethylene copolymers produced via use of vinyl transfer agents and processes for production thereof |
US10676547B2 (en) | 2015-08-31 | 2020-06-09 | Exxonmobil Chemical Patents Inc. | Aluminum alkyls with pendant olefins on clays |
US11041029B2 (en) | 2015-08-31 | 2021-06-22 | Exxonmobil Chemical Patents Inc. | Aluminum alkyls with pendant olefins for polyolefin reactions |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6399535B1 (en) | 1999-11-01 | 2002-06-04 | W. R. Grace & Co.-Conn. | Coordination catalyst systems employing agglomerated metal oxide/clay support-activator and method of their preparation |
US6559090B1 (en) | 1999-11-01 | 2003-05-06 | W. R. Grace & Co.-Conn. | Metallocene and constrained geometry catalyst systems employing agglomerated metal oxide/clay support-activator and method of their preparation |
CN1267191C (zh) * | 1999-12-30 | 2006-08-02 | 菲利浦石油公司 | 有机金属催化剂组合物 |
WO2002022693A1 (fr) * | 2000-09-13 | 2002-03-21 | Japan Polychem Corporation | Catalyseur pour polymerisation d'olefines |
KR100917529B1 (ko) * | 2001-04-30 | 2009-09-16 | 더블유.알. 그레이스 앤드 캄파니-콘. | 지지된 전이 금속 촉매 시스템의 제조 방법 및 그 방법에 의해 제조된 촉매 시스템 |
KR100540049B1 (ko) * | 2001-04-30 | 2006-01-20 | 더블유.알. 그레이스 앤드 캄파니-콘. | 지지된 전이 금속 중합 촉매의 제조 방법 및 이 방법으로형성된 조성물 |
KR100880297B1 (ko) * | 2001-04-30 | 2009-01-28 | 더블유.알. 그레이스 앤드 캄파니-콘. | 크롬 지지체-응집물-전이금속 중합 촉매 및 이의 사용 방법 |
WO2002102859A2 (fr) * | 2001-04-30 | 2002-12-27 | W. R. Grace & Co.-Conn. | Systemes de catalyseur de coordination faisant appel a un agglomerat support de chrome et leur procede de preparation |
US6943224B2 (en) * | 2001-04-30 | 2005-09-13 | W. R. Grace & Co.-Conn. | Process for preparing supported transition metal catalyst systems and catalyst systems prepared thereby |
WO2002088200A1 (fr) * | 2001-04-30 | 2002-11-07 | W.R. Grace & Co.-Conn. | Systemes de catalyseur metallique supporte a transition double |
US6734131B2 (en) | 2001-04-30 | 2004-05-11 | W. R. Grace & Co.-Conn. | Heterogeneous chromium catalysts and processes of polymerization of olefins using same |
WO2003027016A1 (fr) * | 2001-05-22 | 2003-04-03 | The Dow Chemical Company | Nanocomposite contenant des matieres de remplissage fibreuse et lamellaire de dimensions nanometriques |
CN105985458B (zh) * | 2015-02-02 | 2018-12-25 | 中国石油天然气股份有限公司 | 硅胶/粘土复合载体、铬系催化剂、其制法及应用 |
CN105985462B (zh) * | 2015-02-02 | 2018-12-25 | 中国石油天然气股份有限公司 | 粘土改性硅胶复合载体及其制备方法 |
EP3353217A4 (fr) * | 2015-09-24 | 2018-11-07 | ExxonMobil Chemical Patents Inc. | Procédé de polymérisation à l'aide de composés pyridyldiamido supportés sur des supports de silicate stratifié traité par un organoaluminium |
CN106928379B (zh) * | 2015-12-31 | 2020-09-04 | 中国石油天然气股份有限公司 | 聚烯烃用复合载体的制备方法及复合载体的应用 |
CN106076428B (zh) * | 2016-06-16 | 2018-12-28 | 常州大学 | 一种用于脱除重整生成油中微量烯烃的凹土基催化剂的制备方法及应用 |
CN114921236B (zh) * | 2022-05-24 | 2023-02-03 | 中国石油大学(北京) | 一种基于纳米材料缔合的自修复交互网络结构凝胶及其制备方法和应用 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0511665A2 (fr) * | 1991-05-01 | 1992-11-04 | Mitsubishi Chemical Corporation | Catalyseur pour polymérisation d'une oléfine et procédé de production de polymère d'oléfine |
EP0658576A1 (fr) * | 1993-12-17 | 1995-06-21 | Tosoh Corporation | Catalyseur de polymérisation d'oléfines et procédé de polymérisation d'oléfines |
EP0683180A2 (fr) * | 1994-05-18 | 1995-11-22 | Mitsubishi Chemical Corporation | Catalyseur pour la polymérisation d'oléfine et procédé pour la polymérisation d'oléfine |
WO1999047598A1 (fr) * | 1998-03-16 | 1999-09-23 | The Dow Chemical Company | Nanocomposites polyolefiniques |
EP0974601A2 (fr) * | 1998-07-21 | 2000-01-26 | Japan Polychem Corporation | Catalyseur de polymérisation d'oléfines et procédé de préparation de polymères d'oléfines |
WO2000037176A1 (fr) * | 1998-12-22 | 2000-06-29 | W.R. Grace & Co.-Conn. | Procede de fabrication de supports agglomeres cassables seches par atomisation, et catalyseurs de polymerisation olefinique sur ces supports |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4618738A (en) * | 1982-03-09 | 1986-10-21 | Union Oil Company Of California | Hydrocarbon conversion process with catalytically active amorphous silica |
SU1212943A1 (ru) * | 1984-07-09 | 1986-02-23 | Институт общей и неорганической химии АН БССР | Способ получени водостойкого силикагел |
DE3709401A1 (de) * | 1987-03-21 | 1988-09-29 | Huels Chemische Werke Ag | Verfahren zur herstellung eines katalysators fuer die hydratation von olefinen zu alkoholen |
DE3914850A1 (de) * | 1989-05-05 | 1990-11-08 | Basf Ag | Thermisches isoliermaterial auf der basis von pigmenthaltigen kieselsaeureaerogelen |
DE4107973A1 (de) * | 1991-03-13 | 1992-09-17 | Huels Chemische Werke Ag | Verfahren zur herstellung eines katalysators fuer die hydratation von olefinen zu alkoholen |
US5362697A (en) * | 1993-04-26 | 1994-11-08 | Mobil Oil Corp. | Synthetic layered MCM-56, its synthesis and use |
DE19516253A1 (de) * | 1995-04-26 | 1996-10-31 | Grace Gmbh | Mattierungsmittel auf Basis von aggregiertem Siliciumdioxid mit verbesserter Effizienz |
CN1100847C (zh) * | 1999-07-10 | 2003-02-05 | 巴陵石化长岭炼油化工总厂 | 一种烃类催化裂化催化剂的制造方法 |
-
2000
- 2000-10-06 AU AU13307/01A patent/AU1330701A/en not_active Abandoned
- 2000-10-06 AU AU34340/01A patent/AU3434001A/en not_active Abandoned
- 2000-10-06 WO PCT/US2000/027839 patent/WO2001025149A2/fr not_active Application Discontinuation
- 2000-10-06 WO PCT/US2000/027840 patent/WO2001030864A2/fr active Application Filing
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0511665A2 (fr) * | 1991-05-01 | 1992-11-04 | Mitsubishi Chemical Corporation | Catalyseur pour polymérisation d'une oléfine et procédé de production de polymère d'oléfine |
EP0658576A1 (fr) * | 1993-12-17 | 1995-06-21 | Tosoh Corporation | Catalyseur de polymérisation d'oléfines et procédé de polymérisation d'oléfines |
EP0683180A2 (fr) * | 1994-05-18 | 1995-11-22 | Mitsubishi Chemical Corporation | Catalyseur pour la polymérisation d'oléfine et procédé pour la polymérisation d'oléfine |
WO1999047598A1 (fr) * | 1998-03-16 | 1999-09-23 | The Dow Chemical Company | Nanocomposites polyolefiniques |
EP0974601A2 (fr) * | 1998-07-21 | 2000-01-26 | Japan Polychem Corporation | Catalyseur de polymérisation d'oléfines et procédé de préparation de polymères d'oléfines |
WO2000037176A1 (fr) * | 1998-12-22 | 2000-06-29 | W.R. Grace & Co.-Conn. | Procede de fabrication de supports agglomeres cassables seches par atomisation, et catalyseurs de polymerisation olefinique sur ces supports |
Cited By (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6770697B2 (en) | 2001-02-20 | 2004-08-03 | Solvay Engineered Polymers | High melt-strength polyolefin composites and methods for making and using same |
US9283704B2 (en) | 2001-06-18 | 2016-03-15 | Becton, Dickinson And Company | Multilayer containers |
US6583209B2 (en) | 2001-09-06 | 2003-06-24 | Equistar Chemicals, Lp | Propylene polymer composites having improved melt strength |
US8133250B2 (en) | 2001-09-28 | 2012-03-13 | Boston Scientific Scimed, Inc. | Medical devices comprising nanocomposites |
US9463103B2 (en) | 2001-09-28 | 2016-10-11 | Boston Scientific Scimed, Inc. | Medical devices comprising nanocomposites |
US8137373B2 (en) | 2001-09-28 | 2012-03-20 | Boston Scientific Scimed, Inc. | Medical devices comprising nanomaterials and therapeutic methods utilizing the same |
US7517353B2 (en) | 2001-09-28 | 2009-04-14 | Boston Scientific Scimed, Inc. | Medical devices comprising nanomaterials and therapeutic methods utilizing the same |
US7591831B2 (en) | 2001-09-28 | 2009-09-22 | Boston Scientific Scimed, Inc. | Medical devices comprising nanocomposites |
US7037970B2 (en) | 2001-12-20 | 2006-05-02 | Equistar Chemicals, Lp | Process for increasing the melt strength of ethylene-vinyl carboxylate copolymers |
US6646072B2 (en) | 2002-01-23 | 2003-11-11 | Equistar Chemicals, Lp | Process for making polyolefin compositions containing exfoliated clay |
US6979718B2 (en) | 2002-01-23 | 2005-12-27 | Equistar Chemicals, Lp | Process for making polyolefin compositions containing exfoliated clay |
US6942120B2 (en) | 2002-06-07 | 2005-09-13 | S.C. Johnson & Son, Inc. | Disposable bakeware with improved drip resistance at elevated temperatures |
US6884834B2 (en) | 2002-09-19 | 2005-04-26 | Equistar Chemicals, Lp | Shear modification of HDPE-clay nanocomposites |
US7220695B2 (en) | 2004-01-07 | 2007-05-22 | Exxonmobil Chemical Patents Inc. | Supported activator |
US7432319B2 (en) | 2005-11-29 | 2008-10-07 | Honglan Lu | Process for making exfoliated polyolefin/clay nanocomposites |
US7776943B2 (en) | 2006-06-12 | 2010-08-17 | The Regents Of The University Of California | Method for forming exfoliated clay-polyolefin nanocomposites |
US7772299B2 (en) | 2006-06-12 | 2010-08-10 | The Regents Of The University Of California | Method for forming flame-retardant clay-polyolefin composites |
US7754789B1 (en) | 2006-06-12 | 2010-07-13 | The Regents Of The University Of California | Method for forming flame-retardant clay-polyolefin composites |
WO2007146263A3 (fr) * | 2006-06-12 | 2008-02-14 | Univ California | Procédé servant à former des nanocomposites d'argile exfoliée-polyoléfine |
US9321854B2 (en) | 2013-10-29 | 2016-04-26 | Exxonmobil Chemical Patents Inc. | Aluminum alkyl with C5 cyclic and pendent olefin polymerization catalyst |
US10618988B2 (en) | 2015-08-31 | 2020-04-14 | Exxonmobil Chemical Patents Inc. | Branched propylene polymers produced via use of vinyl transfer agents and processes for production thereof |
US10676547B2 (en) | 2015-08-31 | 2020-06-09 | Exxonmobil Chemical Patents Inc. | Aluminum alkyls with pendant olefins on clays |
US11041029B2 (en) | 2015-08-31 | 2021-06-22 | Exxonmobil Chemical Patents Inc. | Aluminum alkyls with pendant olefins for polyolefin reactions |
US10059788B2 (en) | 2016-04-29 | 2018-08-28 | Exxonmobil Chemical Patents Inc. | Organoaluminum activators on clays |
US10562987B2 (en) | 2016-06-30 | 2020-02-18 | Exxonmobil Chemical Patents Inc. | Polymers produced via use of quinolinyldiamido transition metal complexes and vinyl transfer agents |
US10626200B2 (en) | 2017-02-28 | 2020-04-21 | Exxonmobil Chemical Patents Inc. | Branched EPDM polymers produced via use of vinyl transfer agents and processes for production thereof |
US10676551B2 (en) | 2017-03-01 | 2020-06-09 | Exxonmobil Chemical Patents Inc. | Branched ethylene copolymers produced via use of vinyl transfer agents and processes for production thereof |
US10995170B2 (en) | 2017-03-01 | 2021-05-04 | Exxonmobil Chemical Patents Inc. | Branched ethylene copolymers produced via use of vinyl transfer agents and processes for production thereof |
Also Published As
Publication number | Publication date |
---|---|
AU3434001A (en) | 2001-05-08 |
WO2001025149A2 (fr) | 2001-04-12 |
WO2001025149A3 (fr) | 2002-03-14 |
WO2001030864A3 (fr) | 2002-03-28 |
AU1330701A (en) | 2001-05-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2001030864A2 (fr) | Polymeres nanocomposites | |
US6727329B2 (en) | Salts of lewis acid/acid adducts and catalyst activators therefrom | |
US6376421B2 (en) | Ion exchanged aluminum-magnesium silicate or fluorinated magnesium silicate aerogels and catalyst supports therefrom | |
US6255246B1 (en) | Boratabenzene cocatalyst with metallocene catalyst | |
EP1228109B1 (fr) | Catalyseur supporte comprenant des anions expanses | |
US7491672B2 (en) | Chemically-modified supports and supported catalyst systems prepared therefrom | |
US6627573B2 (en) | Expanded anionic compounds comprising hydroxyl or quiescent reactive functionality and catalyst activators therefrom | |
PT863919E (pt) | Catalisador sobre suporte contendo um activador imobilizado que forma catioes | |
WO2001042320A1 (fr) | Compositions a base d'argile traitee et catalyseurs de polymerisation d'olefines les comprenant | |
US6344529B1 (en) | Zwitterionic catalyst activator | |
AU2003233649B2 (en) | Solid, particulated, spray dried, heterogenous catalyst composition | |
JPH10273507A (ja) | プロピレン重合体 | |
WO2003027016A1 (fr) | Nanocomposite contenant des matieres de remplissage fibreuse et lamellaire de dimensions nanometriques | |
EP1412365A1 (fr) | Sel d'acide de lewis/d'adduits acides et activateurs de catalyseur correspondants | |
US20030212222A1 (en) | Chemically -modified supports and supported catalyst systems prepared therefrom | |
MXPA00009379A (es) | Aerogeles de silicato de aluminio-magnesio o silicato de magnesio fluorado con iones intercambiados y soportes de catalizadores de los mismos |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A2 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CR CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A2 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
AK | Designated states |
Kind code of ref document: A3 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CR CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG US UZ YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A3 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG |
|
122 | Ep: pct application non-entry in european phase | ||
NENP | Non-entry into the national phase |
Ref country code: JP |