WO1994010180A1 - Aryloxyaluminoxanes - Google Patents
Aryloxyaluminoxanes Download PDFInfo
- Publication number
- WO1994010180A1 WO1994010180A1 PCT/US1993/010399 US9310399W WO9410180A1 WO 1994010180 A1 WO1994010180 A1 WO 1994010180A1 US 9310399 W US9310399 W US 9310399W WO 9410180 A1 WO9410180 A1 WO 9410180A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- composition
- water
- group
- catalyst system
- halogen
- 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
- B01J31/02—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
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0201—Oxygen-containing compounds
- B01J31/0211—Oxygen-containing compounds with a metal-oxygen link
- B01J31/0214—Aryloxylates, e.g. phenolates
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F5/00—Compounds containing elements of Groups 3 or 13 of the Periodic System
- C07F5/06—Aluminium compounds
- C07F5/061—Aluminium compounds with C-aluminium linkage
- C07F5/066—Aluminium compounds with C-aluminium linkage compounds with Al linked to an element other than Al, C, H or halogen (this includes Al-cyanide linkage)
- C07F5/068—Aluminium compounds with C-aluminium linkage compounds with Al linked to an element other than Al, C, H or halogen (this includes Al-cyanide linkage) preparation of alum(in)oxanes
-
- 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
-
- 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
- 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
Definitions
- Aluminoxanes for example, those of the general formula -(O-AlR) n -, where R is an alkyl group, such as methyl, have received considerable attention in recent years due to their ability to form active olefin polymerization catalysts when combined with Group IV metallocenes.
- R is an alkyl group, such as methyl
- the most important aluminoxane is methylaluminoxane
- Methylaluminoxane is expensive since its synthesis requires the use of a rather expensive
- trimethylaluminum reagent trimethylaluminum reagent. Furthermore, trimethylaluminum is very air- and moisture-sensitive and such factors make them less desirable for large scale industrial applications.
- European Patent Publication No. 561,476 describes the manufacture of polymethylaluminoxane compositions of enhanced solution stability by reaction of the polymethylaluminoxane with certain organic compounds containing heteroatoms such as oxygen. Included as possible compounds are benzyl alcohol, nonyl phenol and butylated hydroxy toluene. The amount of such an organic compound is said to be no more than about 15 wt% of the polyaluminoxane, preferably up to about 10 wt%. Therefore, the resulting compositions, if an aryloxy-containing compound were selected, would contain a minor amount of aryloxy moieties.
- the present invention relates to aryloxyaluminoxanes where an unsubstituted or substituted aryloxy group is directly bonded to the aluminum atom of an aluminoxane so that a predominant amount of aryloxy moieties, such as those comprising an -OC 6 H 5 structure, are a substituent on
- aryloxyaluminoxane as used herein is to be construed as covering aluminoxane compositions which are linear or cyclic and which contain the unit
- n can be an integer of 2 or more and R is an
- aryl such as a phenyl group or a naphthyl group.
- the phenyl group (R) is preferred and can contain at least one suitable electron withdrawing group such as halogen (fluoro, bromo, chloro, or iodo), nitro,
- R trifluoromethyl, cyano, -C(O)R', where R' is alkyl, -C(O)OR", where R" is alkyl, aryl, and the like.
- R is pentafluorophenyl.
- R can be
- alkyl group(s) can be straight chain or branched and can contain from one to twelve carbon atoms.
- the terminology "predominant", and grammatical variants, is intended to distinguish the present materials from those polymethylaluminoxanes described in U.S. Serial No. 853,466 which contain relatively low amounts of aryloxy groups' in certain embodiments (i.e., under about 15 wt%).
- aryloxy substituents preferably about 50% to substantially about 100%.
- linear aluminoxanes in accordance with the present invention have the structure
- R is unsubstituted or substituted aryl, such as phenyl, as described above, and R' can be lower alkyl, such as methyl, or hydroxyl. Both cyclic and acyclic (linear) structures can be present in the aluminoxane product.
- the aryloxyaluminoxanes of this invention can be formed by reacting an organoaluminum compound containing the aryloxy group, for example, of the formula R 2 AlOR', where R can be alkyl, for example, one containing from one to about eight carbon atoms, such as methyl and R' is unsubstituted or substituted aryl, with a source of water, such as liquid water or a compound, such as copper or sodium sulfate having water of crystallization, or silica or alumina, having water of absorption, which can supply the water.
- organoaluminum compound containing the aryloxy group for example, of the formula R 2 AlOR', where R can be alkyl, for example, one containing from one to about eight carbon atoms, such as methyl and R' is unsubstituted or substituted aryl
- a source of water such as liquid water or a compound, such as copper or sodium sulfate having water of crystallization,
- An alternative way to make the aryloxyaluminoxanes of this invention is to react a conventional aluminoxane, such as methylaluminoxane with a reactive compound containing the desired unsubstituted or substituted aryloxy group,
- the aryloxyaluminoxanes of this invention all have utility as cocatalysts for olefin polymerization in Ziegler-Natta and Kaminsky-type catalyst systems based on such catalyst components as unsupported titanium trichloride, supported titanium with and without donor, cyclopentadienyl titanium chlorides, and cyclopentadienyl and substituted cyclopentadienyl zirconium chlorides and alkyls.
- Kaminsky-type systems are preferred. Suitable examples of these preferred systems include zirconocene dichloride, zirconocene dimethyl, bis(pentamethylcyclopentadienyl) dichloride or dimethyl, bis(indenyl) dimethyl, 2,2'-dimethylsila-bis(cyclopentadienyl) zirconium dimethyl, and the like. Still more examples of suitable catalyst
- the present invention is further illustrated by the following Examples.
- This Example illustrates synthesis of. a phenoxy- aliuninoxane.
- Example 1 as a cocatalyst in the polymerization of ethylene.
- This Example illustrates the use of the product from Example 1 as a cocatalyst in the polymerization of propylene.
- This Example illustrates the use of the product from Example 1 as a cocatalyst in the polymerization of propylene.
- This Example illustrates a second route for the
- This Example illustrates the use of the product from Example 5 as a cocatalyst in the polymerization of propylene.
- This Example illustrates the use of the product from Example 5 as a cocatalyst in the isotactic polymerization of propylene.
- metallocenes with various aluminoxanes at a 250:1 molar ratio of Al:Zr All values are given in terms of 10 5 g polypropylene/mole Zr-hr-atm:
- PMAO polymethylaluminoxane. Used as a control and not as part of the present invention.
- Ethylene polymerizations were conducted at 80 °C, three atmospheres pressure, in 250 ml of toluene, with a 3.14 ⁇ 10 5 molar ratio of Al:Zr using dicyclopentadienyl zirconium dichloride as the metallocene:
- This Example is similar to Examples 21-22 but utilizes a phenoxy group with electron donating substituents on the phenyl ring.
Abstract
Aryloxyaluminoxanes containing the unit (I) where R is unsubstituted or substituted aryl, such as phenyl or naphthyl, are useful as cocatalysts in Ziegler-Natta and Kaminsky-type olefin polymerization catalysts. They can be formed by reaction of a source of water with an organoaluminum compound containing the desired aryloxy moiety or by reaction of preformed aluminoxane with an organic compound, such as a phenol, containing such a moiety.
Description
ARYLOXYALUMINOXANES
BACKGROUND OF THE INVENTION
Aluminoxanes, for example, those of the general formula -(O-AlR)n-, where R is an alkyl group, such as methyl, have received considerable attention in recent years due to their ability to form active olefin polymerization catalysts when combined with Group IV metallocenes. Among these, the most important aluminoxane is methylaluminoxane
(R = methyl)' since it produces the highest activity
catalysts. Methylaluminoxane, however, is expensive since its synthesis requires the use of a rather expensive
trimethylaluminum reagent. Furthermore, trimethylaluminum is very air- and moisture-sensitive and such factors make them less desirable for large scale industrial applications.
The disclosures in the art which cover aluminoxane compositions where R, as described above, can be selected from alkyl or, in some cases, aryl, all call for direct bonding of the R group to the aluminum atom. Examples of such disclosures include the following: U.S. Patent Nos. 3,242,099 (R = C1-C12 alkyl or aryl); 4,404,344 (R = C1-C5 alkyl); 4,544,762 (R = C1-C6 alkyl); 4,665,208 (R = C1-C8 alkyl); 4,874,880 (R = hydrocarbyl such as C1-C4 alkyl);
5,041,584 (R = C2 or higher alkyl); and European Patent
Publication No. 324,856 (R = other than n-alkyl such as branched alkyl, cycloalkyl, or aryl).
European Patent Publication No. 561,476 describes the manufacture of polymethylaluminoxane compositions of enhanced solution stability by reaction of the polymethylaluminoxane with certain organic compounds containing heteroatoms such as oxygen. Included as possible compounds are benzyl alcohol, nonyl phenol and butylated hydroxy toluene. The amount of such an organic compound is said to be no more than about 15 wt% of the polyaluminoxane, preferably up to about 10 wt%.
Therefore, the resulting compositions, if an aryloxy-containing compound were selected, would contain a minor amount of aryloxy moieties.
SUMMARY OF THE INVENTION The present invention relates to aryloxyaluminoxanes where an unsubstituted or substituted aryloxy group is directly bonded to the aluminum atom of an aluminoxane so that a predominant amount of aryloxy moieties, such as those comprising an -OC6H5 structure, are a substituent on
aluminum.
DETAILED DESCRIPTION OF THE INVENTION
The term "aryloxyaluminoxane" as used herein is to be construed as covering aluminoxane compositions which are linear or cyclic and which contain the unit
where n can be an integer of 2 or more and R is an
unsubstituted or substituted aryl, such as a phenyl group or a naphthyl group. The phenyl group (R) is preferred and can contain at least one suitable electron withdrawing group such as halogen (fluoro, bromo, chloro, or iodo), nitro,
trifluoromethyl, cyano, -C(O)R', where R' is alkyl, -C(O)OR", where R" is alkyl, aryl, and the like. A preferred selection for R is pentafluorophenyl. Alternatively, R can be
substituted with such electron donating groups as alkyl, alkoxy, or aryloxy. The alkyl group(s) can be straight chain or branched and can contain from one to twelve carbon atoms.
The terminology "predominant", and grammatical variants, is intended to distinguish the present materials from those polymethylaluminoxanes described in U.S. Serial No. 853,466 which contain relatively low amounts of aryloxy groups' in certain embodiments (i.e., under about 15 wt%). In the compositions of the present invention a major amount of the aluminum atoms contain aryloxy substituents, preferably about 50% to substantially about 100%.
It is deemed that linear aluminoxanes in accordance with the present invention have the structure
while cyclic aluminoxanes have the predominant structure
[Al(OR)0]n+2 where R is unsubstituted or substituted aryl, such as phenyl, as described above, and R' can be lower alkyl, such as methyl, or hydroxyl. Both cyclic and acyclic (linear) structures can be present in the aluminoxane product.
The aryloxyaluminoxanes of this invention can be formed by reacting an organoaluminum compound containing the aryloxy group, for example, of the formula R2AlOR', where R can be alkyl, for example, one containing from one to about eight carbon atoms, such as methyl and R' is unsubstituted or substituted aryl, with a source of water, such as liquid water or a compound, such as copper or sodium sulfate having water of crystallization, or silica or alumina, having water of absorption, which can supply the water.
An alternative way to make the aryloxyaluminoxanes of this invention is to react a conventional aluminoxane, such
as methylaluminoxane with a reactive compound containing the desired unsubstituted or substituted aryloxy group,
preferably a phenol.
The aryloxyaluminoxanes of this invention all have utility as cocatalysts for olefin polymerization in Ziegler-Natta and Kaminsky-type catalyst systems based on such catalyst components as unsupported titanium trichloride, supported titanium with and without donor, cyclopentadienyl titanium chlorides, and cyclopentadienyl and substituted cyclopentadienyl zirconium chlorides and alkyls. The
Kaminsky-type systems are preferred. Suitable examples of these preferred systems include zirconocene dichloride, zirconocene dimethyl, bis(pentamethylcyclopentadienyl) dichloride or dimethyl, bis(indenyl) dimethyl, 2,2'-dimethylsila-bis(cyclopentadienyl) zirconium dimethyl, and the like. Still more examples of suitable catalyst
components containing either zirconium or hafnium are
presented in W. Kaminsky, Shokubai. 33, 536 (1991) and J.A. Swen et al., Makromol. Chem., Makromol. Symp., 48/49, 253-295 (1991).
The present invention is further illustrated by the following Examples.
EXAMPLE 1
This Example illustrates synthesis of. a phenoxy- aliuninoxane.
A solution of 1.2 g of Me2AlOC6F5 (D. G. Hendershot et al., organoraetallics, 1991, 10, 1917-1922) in toluene was slowly added to a toluene solution which contained CuSO4· 5H2O (0.4 g, 5 equivalents of OH) at -40P C. The mixture was raised to room temperature over a period of two days with stirring. It was then filtered through a glass frit, and the toluene was removed under vacuum. A white solid was obtained in high yield. The 1H NMR spectrum of this solid product in C6D6 showed no Al-CH3 resonances. The 19F NMR spectrum clearly revealed the presence of -OC6F5 groups.
EXAMPLE 2 This Example illustrates the use of the product from
Example 1 as a cocatalyst in the polymerization of ethylene.
Fifteen milligrams of dicyclopentadienyl zirconium dimethyl was mixed with 100 mg of the white solid obtained from Example 1 (Al/Zr = 11) in 50 mL of dry toluene to yield a homogeneous solution. The solution was then exposed to ethylene (one atmosphere) for fifteen minutes with rapid stirring. After quenching the reaction with methanol, filtering, washing, and drying, 2.0 g of solid polyethylene was obtained.
EXAMPLE 3
This Example illustrates the use of the product from Example 1 as a cocatalyst in the polymerization of propylene.
Six milligrams of dicyσlopentadienyl zirconium dimethyl and 12 mg of the white solid obtained from Example 1 (Al/Zr = 3.5) were mixed in a quartz pressure tube. Then, 4 mL of dry toluene and 10 mL of liquid propylene were condensed into the above tube at -78º C. The reaction mixture was stirred at 0ºC for one hour and then at room temperature for fifty minutes. The reaction was quenched with methanol, and the solvent was removed under vacuum. The polypropylene product (3.6 g) was collected by washing with acetone and drying under vacuum.
EXAMPLE 4
This Example illustrates the use of the product from Example 1 as a cocatalyst in the polymerization of propylene.
Six milligrams of dicyclopentadienyl zirconium dimethyl (Cp'2ZrMe2;Cp' = η5-C5Me5) and 36 mg of the white solid obtained from Example 1 (Al/Zr = 10.5) were mixed in a quartz pressure tube. Then, 4 mL of dry toluene and 10 mL of liquid propylene were condensed into the above tube at -78ºC. The reaction mixture was stirred at 0 C for twenty-five minutes. The reaction was quenched with methanol. After removing the solvent, the polypropylene product (3.4 g) was collected by washing with acetone and drying under vacuum.
EXAMPLE 5
This Example illustrates a second route for the
synthesis of phenoxyaluminoxanes.
A commercial sample of methylaluminoxane (MAO, 0.60 g) was dissolved in 50 mL of toluene in a 500 mL flask and was cooled to -55* C. A solution of pentafluorophenol (1.85 g) in 20 mL of toluene was then added dropwise to the above
solution. It was slowly warmed to room temperature and stirred for ten hours. A white solid in quantitative yield was collected after removing solvent under vacuum.
EXAMPLE 6
This Example illustrates the use of the product from Example 5 as a cocatalyst in the polymerization of propylene.
Six milligrams of dicyclopentadienyl zirconium dimethyl and 40 mg of the white solid obtained from Example 5 (Al/Zr = 12) were mixed in a 50 mL flask. Then 20 mL of propylene was condensed in at -78ºC. The reaction mixture was stirred at 0º C for three hours. The reaction was quenched with
methanol. Solvent was then removed under vacuum. After washing and drying, 3.3 g of polypropylene was collected.
EXAMPLE 7
This Example illustrates the use of the product from Example 5 as a cocatalyst in the isotactic polymerization of propylene.
Six milligrams of Me2Si(C5Me4)(C5H3R*)ZrMe2(R* = (+)-neomenthyl) and 31 mg of the white solid obtained from
Example 5 (Al/Zr = 12.5) were mixed in a 50 mL flask. Then 20 mL of dry propylene was condensed in at -78°C. The reaction mixture was stirred at 0°C for three hours. A reaction was quenched with methanol. Solvent was then removed under vacuum. After washing and drying, 0.80 g of white solid polypropylene was collected, and 13C NMR (1,2,4-trichlorobenzene, 130°C) showed the "mmmmm" pentad in this material at greater than 90%.
EXAMPLES 8-13
The Table set forth below gives the results of propylene polymerizations conducted at 30°C, one atmosphere, in '250 ml of toluene using two differing zirconium-containing
metallocenes with various aluminoxanes at a 250:1 molar ratio of Al:Zr. All values are given in terms of 105 g polypropylene/mole Zr-hr-atm:
Me2A10øF5 Me2AlOøF5
Metallocene PMAO(1) H2O(2) +CuSO4· 5H2O(3)
Cp2ZrMe 0.40(4) 0.40 1.13(5)
Cp2ZrCl2 1.35(6) 0.81 1.07
(1) PMAO = polymethylaluminoxane. Used as a control and not as part of the present invention.
(2) The molar ratio of water to aluminum was 0.4:1.
(3) The molar ratio of water to aluminum was 1:1.
(4) Average of six runs.
(5) Average of runs of 1.07 and 1.19.
(6) Average of five runs.
EXAMPLES 14-17
The following propylene polymerization data was
generated analogous to that shown in Examples 8-13 using less aluminoxane and a higher zirconium content (a 25:1 ratio of Al:Zr) :
Me2A10øF Me2AlOφF5
Metallocene + H2O (1) +CuSO4- 5H2O (2)
Cp2ZrMe2 0.13 0.28
Cp2ZrCl2 0.15 0.22
(1) The molar ratio of water to aluminum was 0.4:1,
(2) The molar ratio of water to aluminum was 1:1.
EXAMPLES 18-20
The Table set forth below gives the results (105 g polypropylene/mole Zr·hr·atm) of other polymerizations of propylene at 30°C, one atmosphere, 250 ml toluene, and 250:1 ratio of Al:Zr:
Aluminoxane Metallocene Used
Used Cp2ZrMe2 Cp2ZrCl2
Et2AlOøF5 + H2O 0.80(1) 0.81 (0.5:l)(2)
(iBu)2AlOφF5 + H2O 0.60
(0.4:1)(2)
(1) Average of runs of 0.71 and 0.89.
(2) This indicates the molar ratio of water to aluminum.
EXAMPLES 21-23
Ethylene polymerizations were conducted at 80 °C, three atmospheres pressure, in 250 ml of toluene, with a 3.14 × 105 molar ratio of Al:Zr using dicyclopentadienyl zirconium dichloride as the metallocene:
Aluminoxane Used Productivity(1)
PMAO 2.35(2)
Me2AlOøF5 + H2O 1.11
(0.4:1) (iBu)2AlOøF5 + H2O
(0.4:1) 0.70
(1) Measured as 106 gm. PE/ gm. Zr hr. atm.
{2) Average of eight runs.
EXAMPLE 24
This Example is similar to Examples 21-22 but utilizes a phenoxy group with electron donating substituents on the phenyl ring. The product of the reaction of
triisobutylaluminum and 2,6-di-t-butyl-paracresol (1:1 mole ratio), or 2,6-di-t-butyl-4-methyl-phenoxide, was converted to an aluminoxane with water (0.65:1 water to aluminum mole ratio). This aluminoxane was used in ethylene polymerization with zirconocene dichloride under the same reaction
conditions used in Examples 21-22. The polyethylene produced amounted to 0.51 × 106 g. PE/ g. Zr.hr. atm.
The foregoing Examples, since they are intended to merely set forth only certain embodiments of the present invention, should not be construed in a limiting sense. The scope of protection sought is set forth in the Claims which follow.
Claims
1. A composition of matter which predominantly
comprises aryloxyaluminoxane and which contains at least one electron withdrawing group or at least one electron donating group.
2. A composition as claimed in Claim 1 which
predominantly comprises phenoxyaluminoxane containing at least one electron withdrawing group.
3. A composition as claimed in Claim 2 wherein the electron withdrawing group is halogen.
4. A composition as claimed in Claim 3 wherein the halogen is fluoro.
5. A composition as claimed in Claim 3 wherein the halogen is chloro.
6. A composition as claimed in Claim 1 which
predominantly comprises phenoxyaluminoxane containing at least one electron donating group.
7. A composition as claimed in Claim 6 herein the electron donating group is alkyl.
8. A process for forming the composition of Claim 1 which comprises reacting an organoaluminum compound
containing the aryloxy group with a source of water.
9. A process as claimed in Claim 8 wherein the source of water is water of crystallization or water of absorption.
10. A process as claimed in Claim 8 wherein the source of water is liquid water.
11. A process for forming the composition of Claim 1 which comprises reacting an aluminoxane with a compound containing the aryloxy group.
12. A process as claimed in Claim 11 wherein the compound is a phenol.
13. A Ziegler-Natta or Kaminsky-type catalyst system for the polymerization of olefins which comprises, as a
cocatalyst, a composition of matter which predominantly comprises aryloxyaluminoxane.
14. A catalyst system as claimed in Claim 13 wherein the composition of matter predominantly comprises phenoxyaluminoxane containing at least one electron withdrawing group.
15. A catalyst system as claimed in Claim 14 wherein the electron withdrawing group is halogen.
16. A catalyst system as claimed in Claim 15 wherein the halogen is fluoro.
17. A catalyst system as claimed in Claim 15 wherein the halogen is chloro.
18. A catalyst system as claimed in Claim 13 wherein the composition of matter predominantly comprises
phenoxyaluminoxane containing at least one electron donating group.
19. A catalyst system as claimed in Claim 18 wherein the electron donating group is alkyl.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/969,920 | 1992-11-02 | ||
US07/969,920 US5391793A (en) | 1992-11-02 | 1992-11-02 | Aryloxyaluminoxanes |
US08/132,736 | 1993-10-06 | ||
US08/132,736 US5939346A (en) | 1992-11-02 | 1993-10-06 | Catalyst system comprising an aryloxyaluminoxane containing an electron withdrawing group |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1994010180A1 true WO1994010180A1 (en) | 1994-05-11 |
Family
ID=26830683
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1993/010399 WO1994010180A1 (en) | 1992-11-02 | 1993-10-29 | Aryloxyaluminoxanes |
Country Status (2)
Country | Link |
---|---|
US (1) | US5939346A (en) |
WO (1) | WO1994010180A1 (en) |
Cited By (174)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996016093A2 (en) | 1994-11-23 | 1996-05-30 | Exxon Chemical Patents Inc. | Method for making supported catalyst systems, and catalyst systems therefrom |
US5786291A (en) * | 1996-02-23 | 1998-07-28 | Exxon Chemical Patents, Inc. | Engineered catalyst systems and methods for their production and use |
US5811379A (en) * | 1996-06-17 | 1998-09-22 | Exxon Chemical Patents Inc. | Polymers derived from olefins useful as lubricant and fuel oil additives, processes for preparation of such polymers and additives and use thereof (PT-1267) |
EP0869103A1 (en) * | 1997-03-31 | 1998-10-07 | David Allan Atwood | Organometallic single source precursors for inorganic films coatings and powders |
WO1999011648A1 (en) * | 1997-08-28 | 1999-03-11 | Zeneca Limited | Organometallic compounds, their preparation and use |
WO1999015534A1 (en) * | 1997-09-19 | 1999-04-01 | The Dow Chemical Company | Modified alumoxane catalyst activator |
WO1999030819A1 (en) * | 1997-12-18 | 1999-06-24 | Mobil Oil Corporation | Olefin polymerisation catalyst based on metallocene complexes and perfluorinated oligoaryl derivatives of aluminates |
WO1999030821A1 (en) * | 1997-12-18 | 1999-06-24 | Mobil Oil Corporation | Catalyst compositions for olefin polymerization based on metallocene complexes and novel cocatalysts produced from trialkylaluminum compounds, sterically hindered phenols, and water |
WO1999061486A1 (en) | 1998-05-29 | 1999-12-02 | Univation Technologies Llc | Catalyst delivery method and catalyst feeder |
US6015766A (en) * | 1997-12-18 | 2000-01-18 | Mobil Oil Corporation | Catalyst systems for olefin polymerization based on metallocene complexes and oligoalkylaluminates with sterically hindered alkyl groups as cocatalysts |
KR20000022955A (en) * | 1998-09-09 | 2000-04-25 | 고오사이 아끼오 | Modified aluminum oxy compound, polymerization catalyst and process for producing olefin polymer and alkenyl aromatic hydrocarbon polymer |
US6066603A (en) * | 1996-06-17 | 2000-05-23 | Exxon Chemical Patents Inc. | Polar monomer containing copolymers derived from olefins useful as lubricant and useful as lubricant and fuel oil additivies process for preparation of such copolymers and additives and use thereof |
US6100213A (en) * | 1996-03-19 | 2000-08-08 | Sumitomo Chemical Company, Limited | Aluminum compound-containing solid catalyst component, catalyst for olefin polymerization and method for producing olefin polymer |
US6117962A (en) * | 1997-12-10 | 2000-09-12 | Exxon Chemical Patents Inc. | Vinyl-containing stereospecific polypropylene macromers |
US6127302A (en) * | 1997-12-09 | 2000-10-03 | Union Carbide Chemicals & Plastics Technology Corporation | Unbridged monocyclopentadienyl metal complex catalyst and a process for polyolefin production |
EP1055673A1 (en) * | 1998-12-10 | 2000-11-29 | Idemitsu Petrochemical Co., Ltd. | Aluminumoxy compound, catalyst component for olefin polymerization and method for producing polyolefin |
US6172015B1 (en) | 1997-07-21 | 2001-01-09 | Exxon Chemical Patents, Inc | Polar monomer containing copolymers derived from olefins useful as lubricant and fuel oil additives, processes for preparation of such copolymers and additives and use thereof |
US6174930B1 (en) | 1999-04-16 | 2001-01-16 | Exxon Chemical Patents, Inc. | Foamable polypropylene polymer |
US6184327B1 (en) | 1997-12-10 | 2001-02-06 | Exxon Chemical Patents, Inc. | Elastomeric propylene polymers |
US6197910B1 (en) | 1997-12-10 | 2001-03-06 | Exxon Chemical Patents, Inc. | Propylene polymers incorporating macromers |
US6207750B1 (en) | 1998-05-13 | 2001-03-27 | Exxon Chemical Patents, Inc. | Propylene homopolymers and methods of making the same |
US6225432B1 (en) | 1998-08-26 | 2001-05-01 | Exxon Chemical Patents Inc. | Branched polypropylene compositions |
US6291387B1 (en) * | 1998-03-20 | 2001-09-18 | Penn State Research Foundation | Transition metal-free olefin polymerization catalyst |
US6306960B1 (en) | 1998-05-13 | 2001-10-23 | Exxonmobil Chemical Patents Inc. | Articles formed from foamable polypropylene polymer |
SG86461A1 (en) * | 2000-03-10 | 2002-02-19 | Sumitomo Chemical Co | Olefin polymerization catalyst and process for producing olefin polymer |
US6380332B1 (en) | 1997-01-28 | 2002-04-30 | Borealis Technology Oy | Activator system for metallocene compounds |
US6403773B1 (en) | 1998-09-30 | 2002-06-11 | Exxon Mobil Chemical Patents Inc. | Cationic group 3 catalyst system |
US6413900B1 (en) | 1995-08-10 | 2002-07-02 | Exxonmobil Chemical Patents Inc. | Metallocene stabilized alumoxane |
US6489416B2 (en) | 1998-03-20 | 2002-12-03 | The Penn State Research Foundation | Process for synthesizing linear polymers of ethylene and alpha-olefins |
WO2003002583A2 (en) | 2001-06-29 | 2003-01-09 | Exxonmobil Chemical Patents Inc. | Metallocenes and catalyst compositions derived therefrom |
US6512019B1 (en) | 1999-11-04 | 2003-01-28 | Exxonmobil Chemical Patents Inc. | Polypropylene copolymer foams and their use |
US6548443B1 (en) | 1999-08-31 | 2003-04-15 | Sumitomo Chemical Company, Limited | Olefin polymerization catalyst and process for producing olefin polymer |
US6555635B2 (en) | 1997-02-07 | 2003-04-29 | Exxonmobil Chemical Patents Inc. | Preparation of vinyl-containing macromers |
US6660809B1 (en) | 1997-02-07 | 2003-12-09 | Exxonmobil Chemical Patents Inc. | Propylene polymers incorporating polyethylene macromers |
US6664208B1 (en) | 1999-09-07 | 2003-12-16 | Sumitomo Chemical Company, Limited | Modified aluminum oxy compound, polymerization catalyst and process for producing olefin polymer and alkenyl aromatic hydrocarbon polymer |
WO2004046214A2 (en) | 2002-10-15 | 2004-06-03 | Exxonmobil Chemical Patents Inc. | Multiple catalyst system for olefin polymerization and polymers produced therefrom |
US6784269B2 (en) | 1998-05-13 | 2004-08-31 | Exxonmobil Chemical Patents Inc. | Polypropylene compositions methods of making the same |
US6809168B2 (en) | 1999-12-10 | 2004-10-26 | Exxonmobil Chemical Patents Inc. | Articles formed from propylene diene copolymers |
WO2004099268A1 (en) | 2003-05-02 | 2004-11-18 | Dow Global Technologies Inc | High activity olefin polymerization catalyst and process |
US6894180B2 (en) | 2002-11-21 | 2005-05-17 | Fina Technology, Inc. | Catalyst structure for olefin polymerization |
WO2005113622A1 (en) | 2004-04-15 | 2005-12-01 | Exxonmobil Chemical Patents Inc. | Multiple catalyst and reactor system for olefin polymerization and polymers produced therefrom |
WO2005118605A1 (en) | 2004-05-26 | 2005-12-15 | Exxonmobil Chemical Patents, Inc. | Transition metal compounds for olefin polymerization and oligomerization |
US6977287B2 (en) | 1999-12-10 | 2005-12-20 | Exxonmobil Chemical Patents Inc. | Propylene diene copolymers |
EP1624000A1 (en) | 1999-05-06 | 2006-02-08 | Univation Technologies, LLC | A polymerization process for producing easier processing polymers |
US7005491B2 (en) | 1999-12-10 | 2006-02-28 | Exxonmobil Chemical Patents Inc. | Propylene diene copolymerized polymers |
WO2006049699A1 (en) | 2004-10-29 | 2006-05-11 | Exxonmobil Chemical Patents Inc | Catalyst compound containing divalent tridentate ligand |
WO2007011832A1 (en) | 2005-07-19 | 2007-01-25 | Exxonmobil Chemical Patents Inc. | Lubricants from mixed alpha-olefin feeds |
US7195806B2 (en) | 2003-01-17 | 2007-03-27 | Fina Technology, Inc. | High gloss polyethylene articles |
WO2007070041A1 (en) | 2005-12-14 | 2007-06-21 | Exxonmobil Chemical Patents Inc. | Halogen substituted metallocene compounds for olefin polymerization |
EP1803747A1 (en) | 2005-12-30 | 2007-07-04 | Borealis Technology Oy | Surface-modified polymerization catalysts for the preparation of low-gel polyolefin films |
WO2007076398A2 (en) * | 2005-12-21 | 2007-07-05 | Albemarle Corporation | Catalyst activators, processes for making same, and use thereof in catalysts and polymerization of olefins |
EP1914252A1 (en) | 1999-12-16 | 2008-04-23 | Univation Technologies, LLC | Method of polymerization |
WO2009035580A1 (en) | 2007-09-13 | 2009-03-19 | Exxonmobil Research And Engineering Company | In-line process for producing plasticized polymers and plasticized polymer blends |
EP2045304A2 (en) | 1999-12-22 | 2009-04-08 | ExxonMobil Chemical Patents Inc. | Polypropylene-Based Adhesive Compositions |
EP2112173A1 (en) | 2008-04-16 | 2009-10-28 | ExxonMobil Chemical Patents Inc. | Catalyst compounds and use thereof |
EP2119732A1 (en) | 2008-05-16 | 2009-11-18 | Borealis Technology Oy | Metallocene catalyst compositions with improved properties, process for its preparation and use for preparing polyolefin homo- or copolymers |
WO2010027491A1 (en) | 2008-09-05 | 2010-03-11 | Exxonmobil Research And Engineering Company | Process for feeding ethylene to polymerization reactors |
EP2172490A1 (en) | 2008-10-03 | 2010-04-07 | Ineos Europe Limited | Controlled polymerisation process |
EP2186832A1 (en) | 2008-11-10 | 2010-05-19 | Borealis AG | Process for the preparation of an unsupported, solid metallocene catalyst system and its use in polymerization of olefins |
EP2186831A1 (en) | 2008-11-10 | 2010-05-19 | Borealis AG | Process for the preparation of an unsupported, solid olefin polymerisation catalyst and use in polymerisation of olefins |
WO2010071798A1 (en) | 2008-12-18 | 2010-06-24 | Univation Technologies, Llc | Method for seed bed treatment for a polymerization reaction |
WO2010074815A1 (en) | 2008-12-15 | 2010-07-01 | Exxonmobil Chemical Patents Inc. | Thermoplastic olefin compositions |
EP2281859A1 (en) | 2004-12-21 | 2011-02-09 | Dow Global Technologies Inc. | Polypropylene-based adhesive compounds |
WO2011048527A1 (en) | 2009-10-19 | 2011-04-28 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds with reduced polymer formation |
WO2011071900A2 (en) | 2009-12-07 | 2011-06-16 | Univation Technologies, Llc | Methods for reducing static charge of a catalyst and methods for using the catalyst to produce polyolefins |
WO2011078923A1 (en) | 2009-12-23 | 2011-06-30 | Univation Technologies, Llc | Methods for producing catalyst systems |
WO2011085937A1 (en) | 2010-01-13 | 2011-07-21 | Ineos Europe Limited | Polymer powder storage and/or transport and/or degassing vessels |
WO2011092266A1 (en) | 2010-01-29 | 2011-08-04 | Borealis Ag | Improving homogeneity in polyethylene blends |
WO2011092264A1 (en) | 2010-01-29 | 2011-08-04 | Borealis Ag | Moulding composition |
WO2011092263A1 (en) | 2010-01-29 | 2011-08-04 | Borealis Ag | Polyethylene moulding composition with improved stress crack/stiffness relationship and impact resistance |
WO2011103402A1 (en) | 2010-02-22 | 2011-08-25 | Univation Technologies, Llc | Catalyst systems and methods for using same to produce polyolefin products |
WO2011103280A1 (en) | 2010-02-18 | 2011-08-25 | Univation Technologies, Llc | Methods for operating a polymerization reactor |
EP2368896A1 (en) | 2010-03-01 | 2011-09-28 | ExxonMobil Chemical Patents Inc. | Mono-indenyl transition metal compounds and polymerization therewith |
EP2383298A1 (en) | 2010-04-30 | 2011-11-02 | Ineos Europe Limited | Polymerization process |
EP2383301A1 (en) | 2010-04-30 | 2011-11-02 | Ineos Europe Limited | Polymerization process |
WO2011138211A1 (en) | 2010-05-07 | 2011-11-10 | Borealis Ag | Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins |
WO2011138212A1 (en) | 2010-05-07 | 2011-11-10 | Borealis Ag | Preparation of a solid catalyst system |
WO2011138214A1 (en) | 2010-05-07 | 2011-11-10 | Borealis Ag | Preparation of a solid catalyst system |
US8058373B2 (en) | 2006-05-17 | 2011-11-15 | Dow Global Technologies Llc | Polypropylene solution polymerization process |
WO2012072417A1 (en) | 2010-11-29 | 2012-06-07 | Ineos Commercial Services Uk Limited | Polymerisation control process |
WO2012074710A1 (en) | 2010-11-30 | 2012-06-07 | Univation Technologies, Llc. | Catalyst composition having improved flow characteristics and methods of making and using the same |
WO2012074709A1 (en) | 2010-11-30 | 2012-06-07 | Univation Technologies, Llc | Processes for the polymerization of olefins with extracted metal carboxylate salts |
WO2012158260A1 (en) | 2011-05-13 | 2012-11-22 | Univation Technologies, Llc | Spray-dried catalyst compositions and polymerization processes employing the same |
EP2535360A1 (en) | 2006-12-20 | 2012-12-19 | ExxonMobil Research and Engineering Company | Process for fluid phase in-line blending of polymers |
US8362163B2 (en) | 2007-03-07 | 2013-01-29 | Dow Global Technologies, Llc | Tethered supported transition metal complex |
WO2013025351A1 (en) | 2011-08-12 | 2013-02-21 | Ineos Usa Llc | Apparatus for stirring polymer particles |
WO2013028283A1 (en) | 2011-08-19 | 2013-02-28 | Univation Technologies, Llc | Catalyst systems and methods for using same to produce polyolefin products |
US8420760B2 (en) | 2007-11-19 | 2013-04-16 | Dow Global Technologies Llc | Long chain branched propylene-alpha-olefin copolymers |
WO2013056979A1 (en) | 2011-10-17 | 2013-04-25 | Ineos Europe Ag | Polymer degassing process control |
WO2013070601A2 (en) | 2011-11-08 | 2013-05-16 | Univation Technologies, Llc | Methods of preparing a catalyst system |
WO2013070602A1 (en) | 2011-11-08 | 2013-05-16 | Univation Technologies, Llc | Methods for producing polyolefins with catalyst systems |
WO2013158225A1 (en) | 2012-04-18 | 2013-10-24 | Exxonmobil Chemical Patents Inc. | Polyolefin compositions and methods of production thereof |
US8614277B2 (en) | 2007-12-20 | 2013-12-24 | Exxonmobil Research And Engineering Company | Polypropylene ethylene-propylene copolymer blends and in-line process to produce them |
WO2014074981A1 (en) | 2012-11-12 | 2014-05-15 | Univation Technologies, Llc | Recycle gas cooler systems for gas-phase polymerization processes |
WO2014106143A1 (en) | 2012-12-28 | 2014-07-03 | Univation Technologies, Llc | Supported catalyst with improved flowability |
WO2014109832A1 (en) | 2013-01-14 | 2014-07-17 | Univation Technologies, Llc | Methods for preparing catalyst systems with increased productivity |
WO2014120494A1 (en) | 2013-01-30 | 2014-08-07 | Univation Technologies, Llc | Processes for making catalyst compositions having improved flow |
WO2014123598A1 (en) | 2013-02-07 | 2014-08-14 | Univation Technologies, Llc | Preparation of polyolefin |
WO2014143421A1 (en) | 2013-03-15 | 2014-09-18 | Univation Technologies, Llc | Tridentate nitrogen based ligands for olefin polymerisation catalysts |
WO2014149361A1 (en) | 2013-03-15 | 2014-09-25 | Univation Technologies, Llc | Ligands for catalysts |
WO2014197169A1 (en) | 2013-06-05 | 2014-12-11 | Univation Technologies, Llc | Protecting phenol groups |
WO2015088624A1 (en) | 2013-12-09 | 2015-06-18 | Univation Technologies, Llc | Feeding polymerization additives to polymerization processes |
EP2915826A1 (en) | 2010-10-21 | 2015-09-09 | Univation Technologies, LLC | Polyethylene and process for production thereof |
WO2015153082A1 (en) | 2014-04-02 | 2015-10-08 | Univation Technologies, Llc | Continuity compositions and methods of making and using the same |
WO2015195189A1 (en) | 2014-06-16 | 2015-12-23 | Univation Technologies, Llc | Polyethylene resins |
WO2016028276A1 (en) | 2014-08-19 | 2016-02-25 | Univation Technologies, Llc | Fluorinated catalyst supports and catalyst systems |
WO2016028278A1 (en) | 2014-08-19 | 2016-02-25 | Univation Technologies, Llc | Fluorinated catalyst supports and catalyst systems |
WO2016028277A1 (en) | 2014-08-19 | 2016-02-25 | Univation Technologies, Llc | Fluorinated catalyst supports and catalyst systems |
WO2016036559A1 (en) * | 2014-09-03 | 2016-03-10 | Univation Technologies, Llc | Catalyst activators, methods of preparation and use in polymerization processes |
US9365663B2 (en) | 2008-03-31 | 2016-06-14 | Exxonmobil Chemical Patents Inc. | Production of shear-stable high viscosity PAO |
WO2016145179A1 (en) | 2015-03-10 | 2016-09-15 | Univation Technologies, Llc | Spray dried catalyst compositions, methods for preparation and use in olefin polymerization processes |
WO2016172110A1 (en) | 2015-04-20 | 2016-10-27 | Univation Technologies, Llc | Bridged bi-aromatic ligands and transition metal compounds prepared therefrom |
WO2016172097A1 (en) | 2015-04-20 | 2016-10-27 | Univation Technologies, Llc | Bridged bi-aromatic ligands and olefin polymerization catalysts prepared therefrom |
WO2016176135A1 (en) | 2015-04-27 | 2016-11-03 | Univation Technologies, Llc | Supported catalyst compositions having improved flow properties and preparation thereof |
WO2016195824A1 (en) | 2015-05-29 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Polymerization process using bridged metallocene compounds supported on organoaluminum treated layered silicate supports |
WO2016197037A1 (en) | 2015-06-05 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Catalyst system comprising supported alumoxane and unsupported alumoxane particles |
WO2016196334A1 (en) | 2015-06-05 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Single reactor production of polymers in gas or slurry phase |
WO2016196339A2 (en) | 2015-06-05 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Production of heterophasic polymers in gas or slurry phase |
WO2017052847A1 (en) | 2015-09-24 | 2017-03-30 | Exxonmobil Chemical Patents Inc. | Polymerization process using pyridyldiamido compounds supported on organoaluminum treated layered silicate supports |
US9637602B2 (en) | 2013-12-18 | 2017-05-02 | Borealis Ag | BOPP film with improved stiffness/toughness balance |
US9670293B2 (en) | 2013-10-29 | 2017-06-06 | Borealis Ag | Solid single site catalysts with high polymerisation activity |
US9670347B2 (en) | 2013-08-14 | 2017-06-06 | Borealis Ag | Propylene composition with improved impact resistance at low temperature |
US9708481B2 (en) | 2013-10-24 | 2017-07-18 | Borealis Ag | Blow molded article based on bimodal random copolymer |
US9751962B2 (en) | 2013-11-22 | 2017-09-05 | Borealis Ag | Low emission propylene homopolymer with high melt flow |
US9777142B2 (en) | 2013-08-21 | 2017-10-03 | Borealis Ag | High flow polyolefin composition with high stiffness and toughness |
US9802394B2 (en) | 2013-10-11 | 2017-10-31 | Borealis Ag | Machine direction oriented film for labels |
US9828698B2 (en) | 2013-12-04 | 2017-11-28 | Borealis Ag | Phthalate-free PP homopolymers for meltblown fibers |
US9890275B2 (en) | 2013-08-21 | 2018-02-13 | Borealis Ag | High flow polyolefin composition with high stiffness and toughness |
EP3309182A2 (en) | 2007-11-15 | 2018-04-18 | Univation Technologies, LLC | Polymerization catalysts, methods of making; methods of using, and polyolefinproducts made therefrom |
US10030109B2 (en) | 2014-02-14 | 2018-07-24 | Borealis Ag | Polypropylene composite |
US10040930B2 (en) | 2013-09-27 | 2018-08-07 | Abu Dhabi Polymers Co. Ltd (Borouge) Llc. | Polymer composition with high XS, high Tm suitable for BOPP processing |
WO2018147968A1 (en) | 2017-02-13 | 2018-08-16 | Univation Technologies, Llc | Bimodal polyethylene resins |
EP3372311A1 (en) | 2007-10-22 | 2018-09-12 | Univation Technologies, LLC | Film comprising a polyethylene composition having improved properties |
US10100185B2 (en) | 2014-02-06 | 2018-10-16 | Borealis Ag | Soft copolymers with high impact strength |
US10100186B2 (en) | 2014-02-06 | 2018-10-16 | Borealis Ag | Soft and transparent impact copolymers |
US10227427B2 (en) | 2014-01-17 | 2019-03-12 | Borealis Ag | Process for preparing propylene/1-butene copolymers |
WO2019122016A1 (en) | 2017-12-21 | 2019-06-27 | Borealis Ag | Process for the preparation of solid catalyst |
WO2019125881A1 (en) | 2017-12-18 | 2019-06-27 | Dow Global Technologies Llc | Zirconocene-titanocene catalyst system |
WO2019125880A1 (en) | 2017-12-18 | 2019-06-27 | Dow Global Technologies Llc | Hafnocene-titanocene catalyst system |
US10421921B2 (en) | 2005-07-19 | 2019-09-24 | Exxonmobil Chemical Patents Inc. | Lubricants from mixed alpha-olefin feeds |
WO2019182746A2 (en) | 2018-03-23 | 2019-09-26 | Univation Technologies, Llc | Catalyst formulations |
WO2019182779A1 (en) | 2018-03-19 | 2019-09-26 | Univation Technologies, Llc | Ethylene/1-hexene copolymer |
WO2019190897A1 (en) | 2018-03-26 | 2019-10-03 | Dow Global Technologies Llc | Spray-dried zirconocene catalyst system |
US10450451B2 (en) | 2014-05-20 | 2019-10-22 | Borealis Ag | Polypropylene composition for automotive interior applications |
US10519259B2 (en) | 2013-10-24 | 2019-12-31 | Borealis Ag | Low melting PP homopolymer with high content of regioerrors and high molecular weight |
WO2020028059A1 (en) | 2018-07-31 | 2020-02-06 | Dow Global Technologies Llc | Polyethylene formulations for large part blow molding applications |
WO2020056119A1 (en) | 2018-09-14 | 2020-03-19 | Fina Technology, Inc. | Polyethylene and controlled rheology polypropylene polymer blends and methods of use |
WO2020096732A1 (en) | 2018-11-06 | 2020-05-14 | Dow Global Technologies Llc | Alkane-soluble non-metallocene precatalysts |
WO2020096735A1 (en) | 2018-11-06 | 2020-05-14 | Dow Global Technologies Llc | Method of olefin polymerization using alkane-soluble non-metallocene precatalyst |
WO2020096734A1 (en) | 2018-11-06 | 2020-05-14 | Dow Global Technologies Llc | Alkane-soluble non-metallocene precatalysts |
WO2020172306A1 (en) | 2019-02-20 | 2020-08-27 | Fina Technology, Inc. | Polymer compositions with low warpage |
WO2020205311A1 (en) | 2019-04-05 | 2020-10-08 | Exxonmobil Chemical Patents Inc. | Broad molecular weight distribution polymer product from loop reactors with intentional thermal gradients |
WO2020205337A1 (en) | 2019-04-05 | 2020-10-08 | Exxonmobil Chemical Patents Inc. | Controlling molecular weight distribution and chemical composition distribution of a polyolefin product |
WO2021034471A1 (en) | 2019-08-16 | 2021-02-25 | Exxonmobil Chemical Patents Inc. | Producing blocks of block copolymer in a separator downstream of a reactor |
WO2021086552A1 (en) | 2019-10-29 | 2021-05-06 | Exxonmobil Chemical Patents Inc. | Production of gradient copolymers using monomer and comonomer concentration gradients in a loop reactor |
WO2021242795A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated post-metallocene catalysts |
WO2021242800A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated post-metallocene catalysts |
WO2021243158A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Chemically converted catalysts |
WO2021243213A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Catalyst systems and processes for producing polyethylene using the same |
WO2021242801A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated hybrid catalysts |
WO2021242792A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated post-metallocene catalysts |
WO2021243214A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Catalyst systems and processes for producing polyethylene using the same |
WO2021243145A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Chemically converted catalysts |
WO2021243211A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Catalyst systems and processes for producing polyethylene using the same |
WO2021242678A1 (en) | 2020-05-29 | 2021-12-02 | Univation Technologies, Llc | Single reactor bimodal polyethylene with improved modulus for extrusion blow molding drum applications |
WO2021247244A2 (en) | 2020-06-03 | 2021-12-09 | Exxonmobil Chemical Patents Inc. | Process for production of thermoplastic vulcanizates using supported catalyst systems and compositions made therefrom |
WO2022031398A1 (en) | 2020-08-05 | 2022-02-10 | Dow Global Technologies Llc | Thermoplastic compositions comprising recycled polymers and articles manufactured therefrom |
WO2022031397A1 (en) | 2020-08-05 | 2022-02-10 | Dow Global Technologies Llc | Thermoplastic compositions comprising bimodal polyethylene and articles manufactured therefrom |
WO2022232123A1 (en) | 2021-04-26 | 2022-11-03 | Fina Technology, Inc. | Thin single-site catalyzed polymer sheets |
WO2023096868A1 (en) | 2021-11-23 | 2023-06-01 | Dow Global Technologies Llc | Supported catalyst systems containing a germanium bridged, anthracenyl substituted bis-biphenyl-phenoxy organometallic compound for making polyethylene and polyethylene copolymer resins in a gas phase polymerization reactor |
WO2023096864A1 (en) | 2021-11-23 | 2023-06-01 | Dow Global Technologies Llc | Supported catalyst systems containing a carbon bridged, anthracenyl substituted bis-biphenyl-phenoxy organometallic compound for making polyethylene and poly ethylene copolymer resins in a gas phase polymerization reactor |
WO2023096865A1 (en) | 2021-11-23 | 2023-06-01 | Dow Global Technologies Llc | Supported catalyst systems containing a silocon bridged, anthracenyl substituted bis-biphenyl-phenoxy organometallic compound for making polyethylene and polyethylene copolymer resins in a gas phase polymerization reactor |
EP4212323A1 (en) | 2014-06-16 | 2023-07-19 | Univation Technologies, LLC | A method of manufacturing a blow molded article |
US11753486B2 (en) | 2017-12-28 | 2023-09-12 | Borealis Ag | Catalyst and preparation thereof |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5384299A (en) * | 1987-01-30 | 1995-01-24 | Exxon Chemical Patents Inc. | Ionic metallocene catalyst compositions |
US6696379B1 (en) * | 1997-09-19 | 2004-02-24 | The Dow Chemical Company | Supported modified alumoxane catalyst activator |
JP2008523145A (en) * | 2004-12-13 | 2008-07-03 | イーライ リリー アンド カンパニー | Spiro derivatives as lipoxygenase inhibitors |
CA2503461A1 (en) * | 2005-04-01 | 2006-10-01 | Nova Chemicals Corporation | Modified (mao + aluminum alkyl) activator |
JP6739435B2 (en) | 2015-01-06 | 2020-08-12 | エスシージー ケミカルズ カンパニー,リミテッド | SiO2-layered double hydroxide microspheres and method for making the same |
GB201608384D0 (en) | 2016-05-12 | 2016-06-29 | Scg Chemicals Co Ltd | Unsymmetrical metallocene catalysts and uses thereof |
US11530279B2 (en) | 2019-04-05 | 2022-12-20 | Exxonmobil Chemicals Patents Inc. | Broad molecular weight distribution polymer product from loop reactors with intentional thermal gradients |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5898428A (en) * | 1982-09-27 | 1983-06-11 | Sumitomo Chem Co Ltd | Preparation of inorganic fiber |
US4544762A (en) * | 1982-11-02 | 1985-10-01 | Hoechst Aktiengesellschaft | Process for the preparation of oligomeric aluminoxanes |
US5084585A (en) * | 1989-02-16 | 1992-01-28 | Idemitsu Kosan Company Limited | Process for preparation of aluminoxane |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2744074A (en) * | 1951-04-18 | 1956-05-01 | Du Pont | Polymeric organic aluminum oxides and method for preparing same |
US3242099A (en) * | 1964-03-27 | 1966-03-22 | Union Carbide Corp | Olefin polymerization catalysts |
IT1039828B (en) * | 1975-07-09 | 1979-12-10 | Montedison Spa | COMPONENTS OF PEARL CATALYSTS POLYMERIZATION OF OLEFINS AND CATALYSTS OBTAINED FROM THEM |
CA1152056A (en) * | 1979-06-11 | 1983-08-16 | Brian L. Goodall | Process for the stereospecific polymerization of an alpha-olefin and an alpha-olefin polymerization catalyst system |
DE3007725A1 (en) * | 1980-02-29 | 1981-09-17 | Hansjörg Prof. Dr. 2000 Hamburg Sinn | METHOD FOR PRODUCING POLYETHYLENE, POLYPROPYLENE AND COPOLYMERS |
JPS58149949A (en) * | 1982-03-02 | 1983-09-06 | Sumitomo Chem Co Ltd | Composition for dissolving polymetalloxane |
US4665208A (en) * | 1985-07-11 | 1987-05-12 | Exxon Chemical Patents Inc. | Process for the preparation of alumoxanes |
JPH0780933B2 (en) * | 1986-11-20 | 1995-08-30 | 三井石油化学工業株式会社 | Olefin Polymerization Method |
US4874880A (en) * | 1987-03-10 | 1989-10-17 | Chisso Corporation | Bis(di-, tri- or tetra-substituted-cyclopentadienyl)-zirconium dihalides |
US5041584A (en) * | 1988-12-02 | 1991-08-20 | Texas Alkyls, Inc. | Modified methylaluminoxane |
US4968827A (en) * | 1989-06-06 | 1990-11-06 | Ethyl Corporation | Alkylaluminoxane process |
US5266544A (en) * | 1989-12-29 | 1993-11-30 | Mitsui Petrochemical Industries, Ltd. | Olefin polymerization catalyst and process for the polymerization of olefins |
TW198726B (en) * | 1989-12-29 | 1993-01-21 | Mitsui Petroleum Chemicals Ind | |
US5003095A (en) * | 1990-03-08 | 1991-03-26 | Ethyl Corporation | Process for preparing methylaluminoxanes |
JP2866434B2 (en) * | 1990-03-20 | 1999-03-08 | 出光興産株式会社 | Method for producing aluminoxane |
JP2657957B2 (en) * | 1990-04-27 | 1997-09-30 | キヤノン株式会社 | Projection device and light irradiation method |
US5235081A (en) * | 1992-03-18 | 1993-08-10 | Ethyl Corporation | Method of removing gel forming materials from methylaluminoxanes |
-
1993
- 1993-10-06 US US08/132,736 patent/US5939346A/en not_active Expired - Fee Related
- 1993-10-29 WO PCT/US1993/010399 patent/WO1994010180A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5898428A (en) * | 1982-09-27 | 1983-06-11 | Sumitomo Chem Co Ltd | Preparation of inorganic fiber |
US4544762A (en) * | 1982-11-02 | 1985-10-01 | Hoechst Aktiengesellschaft | Process for the preparation of oligomeric aluminoxanes |
US5084585A (en) * | 1989-02-16 | 1992-01-28 | Idemitsu Kosan Company Limited | Process for preparation of aluminoxane |
Non-Patent Citations (2)
Title |
---|
CHEMICAL ABSTRACTS, Volume 100, No. 8, issued 20 February 1984, SUMITOMO CHEMICAL CO., LTD., "Inorganic Fibers", see page 267, column 1, Abstract No. 55893g; & JP,A,58 098 428. * |
CHEMICAL ABSTRACTS, Volume 109, No. 25, issued 19 December 1988, KURASHOV et al., "Aluminoxanes-Catalysts for Ortho-Alkylation of Phenols", see page 804, column 2, Abstract No. 230427t; & NEFTEKHIMIYA, 28(2), 176-82. * |
Cited By (218)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996016093A2 (en) | 1994-11-23 | 1996-05-30 | Exxon Chemical Patents Inc. | Method for making supported catalyst systems, and catalyst systems therefrom |
US6413900B1 (en) | 1995-08-10 | 2002-07-02 | Exxonmobil Chemical Patents Inc. | Metallocene stabilized alumoxane |
US5786291A (en) * | 1996-02-23 | 1998-07-28 | Exxon Chemical Patents, Inc. | Engineered catalyst systems and methods for their production and use |
US6333388B1 (en) | 1996-03-19 | 2001-12-25 | Sumitomo Chemical Company, Limited | Aluminum compound-containing solid catalyst component, catalyst for olefin polymerization and method for producing olefin polymer |
US6100213A (en) * | 1996-03-19 | 2000-08-08 | Sumitomo Chemical Company, Limited | Aluminum compound-containing solid catalyst component, catalyst for olefin polymerization and method for producing olefin polymer |
US6468948B1 (en) | 1996-06-17 | 2002-10-22 | Infineum Usa L.P. | Polymers derived from olefins useful as lubricant and fuel oil additives, processes for preparation of such polymers and additives and use thereof (PT-1267) |
US6066603A (en) * | 1996-06-17 | 2000-05-23 | Exxon Chemical Patents Inc. | Polar monomer containing copolymers derived from olefins useful as lubricant and useful as lubricant and fuel oil additivies process for preparation of such copolymers and additives and use thereof |
US5811379A (en) * | 1996-06-17 | 1998-09-22 | Exxon Chemical Patents Inc. | Polymers derived from olefins useful as lubricant and fuel oil additives, processes for preparation of such polymers and additives and use thereof (PT-1267) |
US6380332B1 (en) | 1997-01-28 | 2002-04-30 | Borealis Technology Oy | Activator system for metallocene compounds |
US6660809B1 (en) | 1997-02-07 | 2003-12-09 | Exxonmobil Chemical Patents Inc. | Propylene polymers incorporating polyethylene macromers |
US6555635B2 (en) | 1997-02-07 | 2003-04-29 | Exxonmobil Chemical Patents Inc. | Preparation of vinyl-containing macromers |
EP0869103A1 (en) * | 1997-03-31 | 1998-10-07 | David Allan Atwood | Organometallic single source precursors for inorganic films coatings and powders |
US6172015B1 (en) | 1997-07-21 | 2001-01-09 | Exxon Chemical Patents, Inc | Polar monomer containing copolymers derived from olefins useful as lubricant and fuel oil additives, processes for preparation of such copolymers and additives and use thereof |
WO1999011648A1 (en) * | 1997-08-28 | 1999-03-11 | Zeneca Limited | Organometallic compounds, their preparation and use |
WO1999015534A1 (en) * | 1997-09-19 | 1999-04-01 | The Dow Chemical Company | Modified alumoxane catalyst activator |
US6127302A (en) * | 1997-12-09 | 2000-10-03 | Union Carbide Chemicals & Plastics Technology Corporation | Unbridged monocyclopentadienyl metal complex catalyst and a process for polyolefin production |
US6117962A (en) * | 1997-12-10 | 2000-09-12 | Exxon Chemical Patents Inc. | Vinyl-containing stereospecific polypropylene macromers |
US6423793B1 (en) | 1997-12-10 | 2002-07-23 | Exxonmobil Chemical Patents Inc. | Elastomeric propylene polymers |
US6342574B1 (en) | 1997-12-10 | 2002-01-29 | Exxonmobil Chemical Patents Inc | Propylene polymers incorporating macromers |
US6184327B1 (en) | 1997-12-10 | 2001-02-06 | Exxon Chemical Patents, Inc. | Elastomeric propylene polymers |
US6197910B1 (en) | 1997-12-10 | 2001-03-06 | Exxon Chemical Patents, Inc. | Propylene polymers incorporating macromers |
US6153550A (en) * | 1997-12-18 | 2000-11-28 | Mobile Oil Corporation | Olefin polymerization catalyst based on metallocene complexes and perfluorinated oligoaryl derivatives of aluminates |
WO1999030819A1 (en) * | 1997-12-18 | 1999-06-24 | Mobil Oil Corporation | Olefin polymerisation catalyst based on metallocene complexes and perfluorinated oligoaryl derivatives of aluminates |
WO1999030821A1 (en) * | 1997-12-18 | 1999-06-24 | Mobil Oil Corporation | Catalyst compositions for olefin polymerization based on metallocene complexes and novel cocatalysts produced from trialkylaluminum compounds, sterically hindered phenols, and water |
AU743180B2 (en) * | 1997-12-18 | 2002-01-17 | Exxonmobil Oil Corporation | Olefin polymerisation catalyst based on metallocene complexes and perfluorinated oligoaryl derivatives of aluminates |
US6015766A (en) * | 1997-12-18 | 2000-01-18 | Mobil Oil Corporation | Catalyst systems for olefin polymerization based on metallocene complexes and oligoalkylaluminates with sterically hindered alkyl groups as cocatalysts |
US6291387B1 (en) * | 1998-03-20 | 2001-09-18 | Penn State Research Foundation | Transition metal-free olefin polymerization catalyst |
US6489416B2 (en) | 1998-03-20 | 2002-12-03 | The Penn State Research Foundation | Process for synthesizing linear polymers of ethylene and alpha-olefins |
US6476173B1 (en) | 1998-05-13 | 2002-11-05 | Exxon Mobil Chemical Patents Inc. | Propylene homopolymers and methods of making the same |
US6784269B2 (en) | 1998-05-13 | 2004-08-31 | Exxonmobil Chemical Patents Inc. | Polypropylene compositions methods of making the same |
US6306960B1 (en) | 1998-05-13 | 2001-10-23 | Exxonmobil Chemical Patents Inc. | Articles formed from foamable polypropylene polymer |
US6207750B1 (en) | 1998-05-13 | 2001-03-27 | Exxon Chemical Patents, Inc. | Propylene homopolymers and methods of making the same |
WO1999061486A1 (en) | 1998-05-29 | 1999-12-02 | Univation Technologies Llc | Catalyst delivery method and catalyst feeder |
US6225432B1 (en) | 1998-08-26 | 2001-05-01 | Exxon Chemical Patents Inc. | Branched polypropylene compositions |
KR20000022955A (en) * | 1998-09-09 | 2000-04-25 | 고오사이 아끼오 | Modified aluminum oxy compound, polymerization catalyst and process for producing olefin polymer and alkenyl aromatic hydrocarbon polymer |
US6921800B2 (en) | 1998-09-09 | 2005-07-26 | Sumitomo Chemical Company, Limited | Modified aluminum oxy compound, polymerization catalyst and process for producing olefin polymer and alkenyl |
US7211537B2 (en) | 1998-09-09 | 2007-05-01 | Sumitomo Chemical Company Limited | Modified aluminum oxy compound, polymerization catalyst and process for producing olefin polymer and alkenyl aromatic hydrocarbon polymer |
US6984722B2 (en) | 1998-09-30 | 2006-01-10 | Exxonmobil Chemical Patents Inc. | Cationic group 3 catalyst system |
US6677441B2 (en) | 1998-09-30 | 2004-01-13 | Exxonmobil Chemical Patents Inc. | Cationic group 3 catalyst system |
US6403773B1 (en) | 1998-09-30 | 2002-06-11 | Exxon Mobil Chemical Patents Inc. | Cationic group 3 catalyst system |
EP1055673A1 (en) * | 1998-12-10 | 2000-11-29 | Idemitsu Petrochemical Co., Ltd. | Aluminumoxy compound, catalyst component for olefin polymerization and method for producing polyolefin |
EP1055673A4 (en) * | 1998-12-10 | 2003-05-07 | Idemitsu Petrochemical Co | Aluminumoxy compound, catalyst component for olefin polymerization and method for producing polyolefin |
US6174930B1 (en) | 1999-04-16 | 2001-01-16 | Exxon Chemical Patents, Inc. | Foamable polypropylene polymer |
EP1624000A1 (en) | 1999-05-06 | 2006-02-08 | Univation Technologies, LLC | A polymerization process for producing easier processing polymers |
US6548443B1 (en) | 1999-08-31 | 2003-04-15 | Sumitomo Chemical Company, Limited | Olefin polymerization catalyst and process for producing olefin polymer |
US6664208B1 (en) | 1999-09-07 | 2003-12-16 | Sumitomo Chemical Company, Limited | Modified aluminum oxy compound, polymerization catalyst and process for producing olefin polymer and alkenyl aromatic hydrocarbon polymer |
US6512019B1 (en) | 1999-11-04 | 2003-01-28 | Exxonmobil Chemical Patents Inc. | Polypropylene copolymer foams and their use |
US7005491B2 (en) | 1999-12-10 | 2006-02-28 | Exxonmobil Chemical Patents Inc. | Propylene diene copolymerized polymers |
US6977287B2 (en) | 1999-12-10 | 2005-12-20 | Exxonmobil Chemical Patents Inc. | Propylene diene copolymers |
US6809168B2 (en) | 1999-12-10 | 2004-10-26 | Exxonmobil Chemical Patents Inc. | Articles formed from propylene diene copolymers |
EP1914252A1 (en) | 1999-12-16 | 2008-04-23 | Univation Technologies, LLC | Method of polymerization |
EP2045304A2 (en) | 1999-12-22 | 2009-04-08 | ExxonMobil Chemical Patents Inc. | Polypropylene-Based Adhesive Compositions |
US7521507B2 (en) | 1999-12-22 | 2009-04-21 | Exxonmobil Chemical Patents Inc. | Polypropylene-based adhesive compositions |
SG86461A1 (en) * | 2000-03-10 | 2002-02-19 | Sumitomo Chemical Co | Olefin polymerization catalyst and process for producing olefin polymer |
WO2003002583A2 (en) | 2001-06-29 | 2003-01-09 | Exxonmobil Chemical Patents Inc. | Metallocenes and catalyst compositions derived therefrom |
WO2004046214A2 (en) | 2002-10-15 | 2004-06-03 | Exxonmobil Chemical Patents Inc. | Multiple catalyst system for olefin polymerization and polymers produced therefrom |
US6894180B2 (en) | 2002-11-21 | 2005-05-17 | Fina Technology, Inc. | Catalyst structure for olefin polymerization |
US7195806B2 (en) | 2003-01-17 | 2007-03-27 | Fina Technology, Inc. | High gloss polyethylene articles |
WO2004099268A1 (en) | 2003-05-02 | 2004-11-18 | Dow Global Technologies Inc | High activity olefin polymerization catalyst and process |
WO2005113622A1 (en) | 2004-04-15 | 2005-12-01 | Exxonmobil Chemical Patents Inc. | Multiple catalyst and reactor system for olefin polymerization and polymers produced therefrom |
WO2005118605A1 (en) | 2004-05-26 | 2005-12-15 | Exxonmobil Chemical Patents, Inc. | Transition metal compounds for olefin polymerization and oligomerization |
WO2006049699A1 (en) | 2004-10-29 | 2006-05-11 | Exxonmobil Chemical Patents Inc | Catalyst compound containing divalent tridentate ligand |
EP2281859A1 (en) | 2004-12-21 | 2011-02-09 | Dow Global Technologies Inc. | Polypropylene-based adhesive compounds |
US8536268B2 (en) | 2004-12-21 | 2013-09-17 | Dow Global Technologies Llc | Polypropylene-based adhesive compositions |
US10421921B2 (en) | 2005-07-19 | 2019-09-24 | Exxonmobil Chemical Patents Inc. | Lubricants from mixed alpha-olefin feeds |
WO2007011832A1 (en) | 2005-07-19 | 2007-01-25 | Exxonmobil Chemical Patents Inc. | Lubricants from mixed alpha-olefin feeds |
WO2007070041A1 (en) | 2005-12-14 | 2007-06-21 | Exxonmobil Chemical Patents Inc. | Halogen substituted metallocene compounds for olefin polymerization |
WO2007076398A2 (en) * | 2005-12-21 | 2007-07-05 | Albemarle Corporation | Catalyst activators, processes for making same, and use thereof in catalysts and polymerization of olefins |
WO2007076398A3 (en) * | 2005-12-21 | 2007-11-15 | Albemarle Corp | Catalyst activators, processes for making same, and use thereof in catalysts and polymerization of olefins |
EP1803747A1 (en) | 2005-12-30 | 2007-07-04 | Borealis Technology Oy | Surface-modified polymerization catalysts for the preparation of low-gel polyolefin films |
EP2787013A1 (en) | 2006-05-17 | 2014-10-08 | Dow Global Technologies LLC | Polyolefin solution polymerization process and polymer |
US8058373B2 (en) | 2006-05-17 | 2011-11-15 | Dow Global Technologies Llc | Polypropylene solution polymerization process |
EP2535360A1 (en) | 2006-12-20 | 2012-12-19 | ExxonMobil Research and Engineering Company | Process for fluid phase in-line blending of polymers |
US8362163B2 (en) | 2007-03-07 | 2013-01-29 | Dow Global Technologies, Llc | Tethered supported transition metal complex |
WO2009035580A1 (en) | 2007-09-13 | 2009-03-19 | Exxonmobil Research And Engineering Company | In-line process for producing plasticized polymers and plasticized polymer blends |
EP3372311A1 (en) | 2007-10-22 | 2018-09-12 | Univation Technologies, LLC | Film comprising a polyethylene composition having improved properties |
EP3597294A1 (en) | 2007-10-22 | 2020-01-22 | Univation Technologies, LLC | Polyethylene compositions having improved properties |
EP3309182A2 (en) | 2007-11-15 | 2018-04-18 | Univation Technologies, LLC | Polymerization catalysts, methods of making; methods of using, and polyolefinproducts made therefrom |
US8420760B2 (en) | 2007-11-19 | 2013-04-16 | Dow Global Technologies Llc | Long chain branched propylene-alpha-olefin copolymers |
US8614277B2 (en) | 2007-12-20 | 2013-12-24 | Exxonmobil Research And Engineering Company | Polypropylene ethylene-propylene copolymer blends and in-line process to produce them |
US9365663B2 (en) | 2008-03-31 | 2016-06-14 | Exxonmobil Chemical Patents Inc. | Production of shear-stable high viscosity PAO |
EP2112173A1 (en) | 2008-04-16 | 2009-10-28 | ExxonMobil Chemical Patents Inc. | Catalyst compounds and use thereof |
EP2119732A1 (en) | 2008-05-16 | 2009-11-18 | Borealis Technology Oy | Metallocene catalyst compositions with improved properties, process for its preparation and use for preparing polyolefin homo- or copolymers |
WO2010027491A1 (en) | 2008-09-05 | 2010-03-11 | Exxonmobil Research And Engineering Company | Process for feeding ethylene to polymerization reactors |
EP2172490A1 (en) | 2008-10-03 | 2010-04-07 | Ineos Europe Limited | Controlled polymerisation process |
EP2186831A1 (en) | 2008-11-10 | 2010-05-19 | Borealis AG | Process for the preparation of an unsupported, solid olefin polymerisation catalyst and use in polymerisation of olefins |
US8420562B2 (en) | 2008-11-10 | 2013-04-16 | Borealis Ag | Process for the preparation of an unsupported, solid metallocene catalyst system and its use in polymerization of olefins |
US8394733B2 (en) | 2008-11-10 | 2013-03-12 | Borealis Ag | Process for the preparation of an unsupported, solid olefin polymerisation catalyst and use in polymerisation of olefins |
EP2186832A1 (en) | 2008-11-10 | 2010-05-19 | Borealis AG | Process for the preparation of an unsupported, solid metallocene catalyst system and its use in polymerization of olefins |
WO2010074815A1 (en) | 2008-12-15 | 2010-07-01 | Exxonmobil Chemical Patents Inc. | Thermoplastic olefin compositions |
WO2010071798A1 (en) | 2008-12-18 | 2010-06-24 | Univation Technologies, Llc | Method for seed bed treatment for a polymerization reaction |
WO2011048527A1 (en) | 2009-10-19 | 2011-04-28 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds with reduced polymer formation |
WO2011071900A2 (en) | 2009-12-07 | 2011-06-16 | Univation Technologies, Llc | Methods for reducing static charge of a catalyst and methods for using the catalyst to produce polyolefins |
WO2011078923A1 (en) | 2009-12-23 | 2011-06-30 | Univation Technologies, Llc | Methods for producing catalyst systems |
WO2011085937A1 (en) | 2010-01-13 | 2011-07-21 | Ineos Europe Limited | Polymer powder storage and/or transport and/or degassing vessels |
EP2357035A1 (en) | 2010-01-13 | 2011-08-17 | Ineos Europe Limited | Polymer powder storage and/or transport and/or degassing vessels |
WO2011092266A1 (en) | 2010-01-29 | 2011-08-04 | Borealis Ag | Improving homogeneity in polyethylene blends |
WO2011092264A1 (en) | 2010-01-29 | 2011-08-04 | Borealis Ag | Moulding composition |
WO2011092263A1 (en) | 2010-01-29 | 2011-08-04 | Borealis Ag | Polyethylene moulding composition with improved stress crack/stiffness relationship and impact resistance |
EP2354184A1 (en) | 2010-01-29 | 2011-08-10 | Borealis AG | Polyethylene moulding composition with improved stress crack/stiffness relationship and impact resistance |
EP2354183A1 (en) | 2010-01-29 | 2011-08-10 | Borealis AG | Moulding composition |
WO2011103280A1 (en) | 2010-02-18 | 2011-08-25 | Univation Technologies, Llc | Methods for operating a polymerization reactor |
WO2011103402A1 (en) | 2010-02-22 | 2011-08-25 | Univation Technologies, Llc | Catalyst systems and methods for using same to produce polyolefin products |
EP2368896A1 (en) | 2010-03-01 | 2011-09-28 | ExxonMobil Chemical Patents Inc. | Mono-indenyl transition metal compounds and polymerization therewith |
EP2383301A1 (en) | 2010-04-30 | 2011-11-02 | Ineos Europe Limited | Polymerization process |
EP2383298A1 (en) | 2010-04-30 | 2011-11-02 | Ineos Europe Limited | Polymerization process |
WO2011134798A1 (en) | 2010-04-30 | 2011-11-03 | Ineos Commercial Services Uk Limited | Polymerization process |
WO2011134797A1 (en) | 2010-04-30 | 2011-11-03 | Ineos Commercial Services Uk Limited | Polymerization process |
EP2386581A1 (en) | 2010-05-07 | 2011-11-16 | Borealis AG | Preparation of a solid catalyst system |
EP2386583A1 (en) | 2010-05-07 | 2011-11-16 | Borealis AG | Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins |
WO2011138212A1 (en) | 2010-05-07 | 2011-11-10 | Borealis Ag | Preparation of a solid catalyst system |
EP2386582A1 (en) | 2010-05-07 | 2011-11-16 | Borealis AG | Preparation of a solid catalyst system |
WO2011138211A1 (en) | 2010-05-07 | 2011-11-10 | Borealis Ag | Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins |
WO2011138214A1 (en) | 2010-05-07 | 2011-11-10 | Borealis Ag | Preparation of a solid catalyst system |
US8962509B2 (en) | 2010-05-07 | 2015-02-24 | Borealis Ag | Preparation of a solid catalyst system |
EP2915826A1 (en) | 2010-10-21 | 2015-09-09 | Univation Technologies, LLC | Polyethylene and process for production thereof |
WO2012072417A1 (en) | 2010-11-29 | 2012-06-07 | Ineos Commercial Services Uk Limited | Polymerisation control process |
WO2012074709A1 (en) | 2010-11-30 | 2012-06-07 | Univation Technologies, Llc | Processes for the polymerization of olefins with extracted metal carboxylate salts |
WO2012074710A1 (en) | 2010-11-30 | 2012-06-07 | Univation Technologies, Llc. | Catalyst composition having improved flow characteristics and methods of making and using the same |
WO2012158260A1 (en) | 2011-05-13 | 2012-11-22 | Univation Technologies, Llc | Spray-dried catalyst compositions and polymerization processes employing the same |
WO2013025351A1 (en) | 2011-08-12 | 2013-02-21 | Ineos Usa Llc | Apparatus for stirring polymer particles |
WO2013028283A1 (en) | 2011-08-19 | 2013-02-28 | Univation Technologies, Llc | Catalyst systems and methods for using same to produce polyolefin products |
WO2013056979A1 (en) | 2011-10-17 | 2013-04-25 | Ineos Europe Ag | Polymer degassing process control |
WO2013070602A1 (en) | 2011-11-08 | 2013-05-16 | Univation Technologies, Llc | Methods for producing polyolefins with catalyst systems |
US9234060B2 (en) | 2011-11-08 | 2016-01-12 | Univation Technologies, Llc | Methods of preparing a catalyst system |
US9181371B2 (en) | 2011-11-08 | 2015-11-10 | Univation Technologies, Llc | Methods for producing polyolefins with catalyst systems |
WO2013070601A2 (en) | 2011-11-08 | 2013-05-16 | Univation Technologies, Llc | Methods of preparing a catalyst system |
WO2013158225A1 (en) | 2012-04-18 | 2013-10-24 | Exxonmobil Chemical Patents Inc. | Polyolefin compositions and methods of production thereof |
WO2014074981A1 (en) | 2012-11-12 | 2014-05-15 | Univation Technologies, Llc | Recycle gas cooler systems for gas-phase polymerization processes |
WO2014106143A1 (en) | 2012-12-28 | 2014-07-03 | Univation Technologies, Llc | Supported catalyst with improved flowability |
EP4039366A1 (en) | 2012-12-28 | 2022-08-10 | Univation Technologies, LLC | Supported catalyst with improved flowability |
WO2014109832A1 (en) | 2013-01-14 | 2014-07-17 | Univation Technologies, Llc | Methods for preparing catalyst systems with increased productivity |
WO2014120494A1 (en) | 2013-01-30 | 2014-08-07 | Univation Technologies, Llc | Processes for making catalyst compositions having improved flow |
EP4223802A2 (en) | 2013-02-07 | 2023-08-09 | Univation Technologies, LLC | Polymerization catalyst |
WO2014123598A1 (en) | 2013-02-07 | 2014-08-14 | Univation Technologies, Llc | Preparation of polyolefin |
WO2014149361A1 (en) | 2013-03-15 | 2014-09-25 | Univation Technologies, Llc | Ligands for catalysts |
WO2014143421A1 (en) | 2013-03-15 | 2014-09-18 | Univation Technologies, Llc | Tridentate nitrogen based ligands for olefin polymerisation catalysts |
WO2014197169A1 (en) | 2013-06-05 | 2014-12-11 | Univation Technologies, Llc | Protecting phenol groups |
EP3287473A1 (en) | 2013-06-05 | 2018-02-28 | Univation Technologies, LLC | Protecting phenol groups |
US9670347B2 (en) | 2013-08-14 | 2017-06-06 | Borealis Ag | Propylene composition with improved impact resistance at low temperature |
US9777142B2 (en) | 2013-08-21 | 2017-10-03 | Borealis Ag | High flow polyolefin composition with high stiffness and toughness |
US9890275B2 (en) | 2013-08-21 | 2018-02-13 | Borealis Ag | High flow polyolefin composition with high stiffness and toughness |
US10040930B2 (en) | 2013-09-27 | 2018-08-07 | Abu Dhabi Polymers Co. Ltd (Borouge) Llc. | Polymer composition with high XS, high Tm suitable for BOPP processing |
US9802394B2 (en) | 2013-10-11 | 2017-10-31 | Borealis Ag | Machine direction oriented film for labels |
US9708481B2 (en) | 2013-10-24 | 2017-07-18 | Borealis Ag | Blow molded article based on bimodal random copolymer |
US10519259B2 (en) | 2013-10-24 | 2019-12-31 | Borealis Ag | Low melting PP homopolymer with high content of regioerrors and high molecular weight |
US9670293B2 (en) | 2013-10-29 | 2017-06-06 | Borealis Ag | Solid single site catalysts with high polymerisation activity |
US9751962B2 (en) | 2013-11-22 | 2017-09-05 | Borealis Ag | Low emission propylene homopolymer with high melt flow |
US9828698B2 (en) | 2013-12-04 | 2017-11-28 | Borealis Ag | Phthalate-free PP homopolymers for meltblown fibers |
WO2015088624A1 (en) | 2013-12-09 | 2015-06-18 | Univation Technologies, Llc | Feeding polymerization additives to polymerization processes |
US9809656B2 (en) | 2013-12-09 | 2017-11-07 | Univation Technologies, Llc | Feeding polymerization additives to polymerization processes |
US9637602B2 (en) | 2013-12-18 | 2017-05-02 | Borealis Ag | BOPP film with improved stiffness/toughness balance |
US10227427B2 (en) | 2014-01-17 | 2019-03-12 | Borealis Ag | Process for preparing propylene/1-butene copolymers |
US10100186B2 (en) | 2014-02-06 | 2018-10-16 | Borealis Ag | Soft and transparent impact copolymers |
US10100185B2 (en) | 2014-02-06 | 2018-10-16 | Borealis Ag | Soft copolymers with high impact strength |
US10030109B2 (en) | 2014-02-14 | 2018-07-24 | Borealis Ag | Polypropylene composite |
EP3747913A1 (en) | 2014-04-02 | 2020-12-09 | Univation Technologies, LLC | Continuity compositions and olefin polymerisation method using the same |
WO2015153082A1 (en) | 2014-04-02 | 2015-10-08 | Univation Technologies, Llc | Continuity compositions and methods of making and using the same |
US10450451B2 (en) | 2014-05-20 | 2019-10-22 | Borealis Ag | Polypropylene composition for automotive interior applications |
WO2015195189A1 (en) | 2014-06-16 | 2015-12-23 | Univation Technologies, Llc | Polyethylene resins |
EP4212323A1 (en) | 2014-06-16 | 2023-07-19 | Univation Technologies, LLC | A method of manufacturing a blow molded article |
WO2016028276A1 (en) | 2014-08-19 | 2016-02-25 | Univation Technologies, Llc | Fluorinated catalyst supports and catalyst systems |
WO2016028278A1 (en) | 2014-08-19 | 2016-02-25 | Univation Technologies, Llc | Fluorinated catalyst supports and catalyst systems |
WO2016028277A1 (en) | 2014-08-19 | 2016-02-25 | Univation Technologies, Llc | Fluorinated catalyst supports and catalyst systems |
WO2016036559A1 (en) * | 2014-09-03 | 2016-03-10 | Univation Technologies, Llc | Catalyst activators, methods of preparation and use in polymerization processes |
WO2016145179A1 (en) | 2015-03-10 | 2016-09-15 | Univation Technologies, Llc | Spray dried catalyst compositions, methods for preparation and use in olefin polymerization processes |
WO2016172097A1 (en) | 2015-04-20 | 2016-10-27 | Univation Technologies, Llc | Bridged bi-aromatic ligands and olefin polymerization catalysts prepared therefrom |
WO2016172110A1 (en) | 2015-04-20 | 2016-10-27 | Univation Technologies, Llc | Bridged bi-aromatic ligands and transition metal compounds prepared therefrom |
WO2016176135A1 (en) | 2015-04-27 | 2016-11-03 | Univation Technologies, Llc | Supported catalyst compositions having improved flow properties and preparation thereof |
WO2016195824A1 (en) | 2015-05-29 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Polymerization process using bridged metallocene compounds supported on organoaluminum treated layered silicate supports |
WO2016197037A1 (en) | 2015-06-05 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Catalyst system comprising supported alumoxane and unsupported alumoxane particles |
EP3885373A1 (en) | 2015-06-05 | 2021-09-29 | ExxonMobil Chemical Patents Inc. | Production of heterophasic polymers in gas or slurry phase |
WO2016196334A1 (en) | 2015-06-05 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Single reactor production of polymers in gas or slurry phase |
WO2016196339A2 (en) | 2015-06-05 | 2016-12-08 | Exxonmobil Chemical Patents Inc. | Production of heterophasic polymers in gas or slurry phase |
WO2017052847A1 (en) | 2015-09-24 | 2017-03-30 | Exxonmobil Chemical Patents Inc. | Polymerization process using pyridyldiamido compounds supported on organoaluminum treated layered silicate supports |
WO2018147968A1 (en) | 2017-02-13 | 2018-08-16 | Univation Technologies, Llc | Bimodal polyethylene resins |
WO2019125881A1 (en) | 2017-12-18 | 2019-06-27 | Dow Global Technologies Llc | Zirconocene-titanocene catalyst system |
US11421051B2 (en) | 2017-12-18 | 2022-08-23 | Dow Global Technologies Llc | Zirconocene-titanocene catalyst system |
WO2019125880A1 (en) | 2017-12-18 | 2019-06-27 | Dow Global Technologies Llc | Hafnocene-titanocene catalyst system |
US11384170B2 (en) | 2017-12-21 | 2022-07-12 | Borealis Ag | Process for the preparation of solid catalyst |
WO2019122016A1 (en) | 2017-12-21 | 2019-06-27 | Borealis Ag | Process for the preparation of solid catalyst |
US11753486B2 (en) | 2017-12-28 | 2023-09-12 | Borealis Ag | Catalyst and preparation thereof |
US11142600B2 (en) | 2018-03-19 | 2021-10-12 | Univation Technologies, Llc | Ethylene/1-hexene copolymer |
WO2019182779A1 (en) | 2018-03-19 | 2019-09-26 | Univation Technologies, Llc | Ethylene/1-hexene copolymer |
WO2019182746A2 (en) | 2018-03-23 | 2019-09-26 | Univation Technologies, Llc | Catalyst formulations |
WO2019190897A1 (en) | 2018-03-26 | 2019-10-03 | Dow Global Technologies Llc | Spray-dried zirconocene catalyst system |
WO2020028059A1 (en) | 2018-07-31 | 2020-02-06 | Dow Global Technologies Llc | Polyethylene formulations for large part blow molding applications |
US11685798B2 (en) | 2018-07-31 | 2023-06-27 | Dow Global Technologies Llc | Polyethylene formulations for large part blow molding applications |
WO2020056119A1 (en) | 2018-09-14 | 2020-03-19 | Fina Technology, Inc. | Polyethylene and controlled rheology polypropylene polymer blends and methods of use |
US11891464B2 (en) | 2018-11-06 | 2024-02-06 | Dow Global Technologies Llc | Alkane-soluble non-metallocene precatalysts |
US11859031B2 (en) | 2018-11-06 | 2024-01-02 | Dow Global Technologies Llc | Alkane-soluble non-metallocene precatalysts |
WO2020096734A1 (en) | 2018-11-06 | 2020-05-14 | Dow Global Technologies Llc | Alkane-soluble non-metallocene precatalysts |
WO2020096735A1 (en) | 2018-11-06 | 2020-05-14 | Dow Global Technologies Llc | Method of olefin polymerization using alkane-soluble non-metallocene precatalyst |
WO2020096732A1 (en) | 2018-11-06 | 2020-05-14 | Dow Global Technologies Llc | Alkane-soluble non-metallocene precatalysts |
WO2020172306A1 (en) | 2019-02-20 | 2020-08-27 | Fina Technology, Inc. | Polymer compositions with low warpage |
WO2020205337A1 (en) | 2019-04-05 | 2020-10-08 | Exxonmobil Chemical Patents Inc. | Controlling molecular weight distribution and chemical composition distribution of a polyolefin product |
WO2020205311A1 (en) | 2019-04-05 | 2020-10-08 | Exxonmobil Chemical Patents Inc. | Broad molecular weight distribution polymer product from loop reactors with intentional thermal gradients |
WO2021034471A1 (en) | 2019-08-16 | 2021-02-25 | Exxonmobil Chemical Patents Inc. | Producing blocks of block copolymer in a separator downstream of a reactor |
WO2021086552A1 (en) | 2019-10-29 | 2021-05-06 | Exxonmobil Chemical Patents Inc. | Production of gradient copolymers using monomer and comonomer concentration gradients in a loop reactor |
WO2021242800A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated post-metallocene catalysts |
WO2021243211A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Catalyst systems and processes for producing polyethylene using the same |
WO2021242678A1 (en) | 2020-05-29 | 2021-12-02 | Univation Technologies, Llc | Single reactor bimodal polyethylene with improved modulus for extrusion blow molding drum applications |
WO2021243222A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Catalyst systems and processes for producing polyethylene using the same |
WO2021242795A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated post-metallocene catalysts |
WO2021243216A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Spray-dried catalysts containing a germanium-bridged bis-biphenyl-phenoxy organometallic compound for making ethylene-based copolymers |
WO2021243145A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Chemically converted catalysts |
WO2021243214A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Catalyst systems and processes for producing polyethylene using the same |
WO2021242792A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated post-metallocene catalysts |
WO2021243158A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Chemically converted catalysts |
WO2021243213A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Catalyst systems and processes for producing polyethylene using the same |
WO2021242801A1 (en) | 2020-05-29 | 2021-12-02 | Dow Global Technologies Llc | Attenuated hybrid catalysts |
WO2021247244A2 (en) | 2020-06-03 | 2021-12-09 | Exxonmobil Chemical Patents Inc. | Process for production of thermoplastic vulcanizates using supported catalyst systems and compositions made therefrom |
WO2022031398A1 (en) | 2020-08-05 | 2022-02-10 | Dow Global Technologies Llc | Thermoplastic compositions comprising recycled polymers and articles manufactured therefrom |
WO2022031397A1 (en) | 2020-08-05 | 2022-02-10 | Dow Global Technologies Llc | Thermoplastic compositions comprising bimodal polyethylene and articles manufactured therefrom |
WO2022232123A1 (en) | 2021-04-26 | 2022-11-03 | Fina Technology, Inc. | Thin single-site catalyzed polymer sheets |
WO2023096865A1 (en) | 2021-11-23 | 2023-06-01 | Dow Global Technologies Llc | Supported catalyst systems containing a silocon bridged, anthracenyl substituted bis-biphenyl-phenoxy organometallic compound for making polyethylene and polyethylene copolymer resins in a gas phase polymerization reactor |
WO2023096864A1 (en) | 2021-11-23 | 2023-06-01 | Dow Global Technologies Llc | Supported catalyst systems containing a carbon bridged, anthracenyl substituted bis-biphenyl-phenoxy organometallic compound for making polyethylene and poly ethylene copolymer resins in a gas phase polymerization reactor |
WO2023096868A1 (en) | 2021-11-23 | 2023-06-01 | Dow Global Technologies Llc | Supported catalyst systems containing a germanium bridged, anthracenyl substituted bis-biphenyl-phenoxy organometallic compound for making polyethylene and polyethylene copolymer resins in a gas phase polymerization reactor |
Also Published As
Publication number | Publication date |
---|---|
US5939346A (en) | 1999-08-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5391793A (en) | Aryloxyaluminoxanes | |
US5939346A (en) | Catalyst system comprising an aryloxyaluminoxane containing an electron withdrawing group | |
US6355819B1 (en) | Substituted metallocene compounds for olefin polymerization catalyst systems, their intermediates and methods for preparing them | |
KR100348379B1 (en) | Uncrosslinked indenyl-containing metallocene | |
EP1363955B1 (en) | Multinuclear metallocene catalyst | |
US5583189A (en) | Polymerization processes | |
US5561092A (en) | Metallocene catalysts with lewis acids and aluminum alkyls | |
US6417302B1 (en) | Compounds containing boron and aluminium | |
KR100309224B1 (en) | Method for preparing solid organic-aluminoxyl product useful for polymerization catalyst | |
US5886202A (en) | Bridged fluorenyl/indenyl metallocenes and the use thereof | |
KR20020034193A (en) | Catalyst system and process for the polymerization of olefins | |
US5202398A (en) | Process for the preparation of a 1-olefin polymer | |
JP2003105014A (en) | Method for adjusting syndiotactic polyolefin melting point and molecular weight by using metallocene catalyst | |
JP2003534346A (en) | Chemical products suitable as cocatalysts, their preparation and use in catalyst compositions for the production of polyolefins | |
KR19980033355A (en) | Metallocene | |
US5384298A (en) | Catalyst for polymerization of olefin and process for production of olefin polymer | |
EP0645393B1 (en) | Aluminoxanes having increased catalytic activity | |
US5457171A (en) | Catalyst systems for the polymerization of C2 -C10 -alkenes | |
US6262201B1 (en) | Aryl substituted metallocene catalysts and their use | |
US5726264A (en) | Processes to produce metallocene compounds and polymerization processes therewith | |
KR100404780B1 (en) | Metallocene compounds, metallocene catalysts prepared from the compounds and method of polymerizing olefins with the catalysts | |
US5770666A (en) | Organic transition metal compound and process for the preparation of polyolefin using same | |
EP0269002A2 (en) | Fluoroalkoxyaluminium compounds and their use in polymerization processes | |
JP3382882B2 (en) | Heterogeneous catalyst component and polymerization method of α-olefin | |
KR100417970B1 (en) | Crosslinking metallocenes useful for olefin polymerization catalyst systems |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): JP |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE |
|
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) | ||
122 | Ep: pct application non-entry in european phase |