US20020010080A1 - Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations - Google Patents
Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations Download PDFInfo
- Publication number
- US20020010080A1 US20020010080A1 US09/899,698 US89969801A US2002010080A1 US 20020010080 A1 US20020010080 A1 US 20020010080A1 US 89969801 A US89969801 A US 89969801A US 2002010080 A1 US2002010080 A1 US 2002010080A1
- Authority
- US
- United States
- Prior art keywords
- complex
- fluorinated
- formula
- mepbb
- mebr
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002841 Lewis acid Substances 0.000 title claims abstract description 10
- 125000002091 cationic group Chemical group 0.000 title abstract description 5
- 238000006116 polymerization reaction Methods 0.000 title description 23
- 150000001336 alkenes Chemical class 0.000 title description 6
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 title description 5
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical group C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 claims abstract description 39
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical group [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052796 boron Inorganic materials 0.000 claims abstract description 22
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims abstract description 20
- 125000003367 polycyclic group Chemical group 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims description 41
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 41
- 239000003054 catalyst Substances 0.000 claims description 33
- 229910052739 hydrogen Inorganic materials 0.000 claims description 29
- 230000003197 catalytic effect Effects 0.000 claims description 27
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 claims description 21
- 125000000217 alkyl group Chemical group 0.000 claims description 20
- 125000003118 aryl group Chemical group 0.000 claims description 19
- 229910052726 zirconium Inorganic materials 0.000 claims description 18
- 229910052735 hafnium Inorganic materials 0.000 claims description 16
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 15
- 239000005977 Ethylene Substances 0.000 claims description 15
- 229910052776 Thorium Inorganic materials 0.000 claims description 15
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 claims description 15
- SMPRZROHMIPVJH-NCOIDOBVSA-N pCpC Chemical compound O=C1N=C(N)C=CN1[C@H]1[C@H](O)[C@H](O)[C@@H](COP(O)(=O)O[C@H]2[C@H]([C@@H](O[C@@H]2COP(O)(O)=O)N2C(N=C(N)C=C2)=O)O)O1 SMPRZROHMIPVJH-NCOIDOBVSA-N 0.000 claims description 15
- -1 5-cyclopentadienyl Chemical group 0.000 claims description 14
- 239000004711 α-olefin Substances 0.000 claims description 11
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 8
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 8
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 8
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 8
- YBYIRNPNPLQARY-UHFFFAOYSA-N 1H-indene Natural products C1=CC=C2CC=CC2=C1 YBYIRNPNPLQARY-UHFFFAOYSA-N 0.000 claims description 5
- 125000003454 indenyl group Chemical group C1(C=CC2=CC=CC=C12)* 0.000 claims description 5
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 4
- 235000010290 biphenyl Nutrition 0.000 claims description 4
- 150000004074 biphenyls Chemical class 0.000 claims description 4
- 125000001624 naphthyl group Chemical group 0.000 claims description 4
- 229920000642 polymer Polymers 0.000 claims description 4
- FAQYAMRNWDIXMY-UHFFFAOYSA-N trichloroborane Chemical group ClB(Cl)Cl FAQYAMRNWDIXMY-UHFFFAOYSA-N 0.000 claims description 4
- 235000019000 fluorine Nutrition 0.000 claims description 3
- 125000001153 fluoro group Chemical group F* 0.000 claims description 3
- 229920000909 polytetrahydrofuran Polymers 0.000 claims description 3
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical group [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 2
- 125000002178 anthracenyl group Chemical group C1(=CC=CC2=CC3=CC=CC=C3C=C12)* 0.000 claims description 2
- 125000003983 fluorenyl group Chemical group C1(=CC=CC=2C3=CC=CC=C3CC12)* 0.000 claims description 2
- 239000012454 non-polar solvent Substances 0.000 claims description 2
- GZUXJHMPEANEGY-UHFFFAOYSA-N bromomethane Chemical compound BrC GZUXJHMPEANEGY-UHFFFAOYSA-N 0.000 claims 25
- 125000004432 carbon atom Chemical group C* 0.000 claims 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 8
- UORVGPXVDQYIDP-UHFFFAOYSA-N borane Chemical compound B UORVGPXVDQYIDP-UHFFFAOYSA-N 0.000 claims 4
- 229910052757 nitrogen Inorganic materials 0.000 claims 4
- IPRROFRGPQGDOX-UHFFFAOYSA-K 1,2,3,4,5-pentamethylcyclopenta-1,3-diene;trichlorotitanium Chemical group Cl[Ti](Cl)Cl.CC=1C(C)=C(C)[C-](C)C=1C IPRROFRGPQGDOX-UHFFFAOYSA-K 0.000 claims 3
- 239000000243 solution Substances 0.000 claims 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 2
- 239000007983 Tris buffer Substances 0.000 claims 2
- 229910000085 borane Inorganic materials 0.000 claims 2
- 239000001257 hydrogen Substances 0.000 claims 2
- 230000000379 polymerizing effect Effects 0.000 claims 2
- 125000003808 silyl group Chemical group [H][Si]([H])([H])[*] 0.000 claims 2
- 229920000098 polyolefin Polymers 0.000 claims 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims 1
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 claims 1
- 239000002685 polymerization catalyst Substances 0.000 abstract description 4
- UHOVQNZJYSORNB-MZWXYZOWSA-N benzene-d6 Chemical compound [2H]C1=C([2H])C([2H])=C([2H])C([2H])=C1[2H] UHOVQNZJYSORNB-MZWXYZOWSA-N 0.000 description 35
- 238000006243 chemical reaction Methods 0.000 description 30
- XSQNOFMFKVYSNL-UHFFFAOYSA-N ethene;toluene Chemical group C=C.CC1=CC=CC=C1 XSQNOFMFKVYSNL-UHFFFAOYSA-N 0.000 description 16
- 238000005160 1H NMR spectroscopy Methods 0.000 description 13
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 13
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 12
- 238000004293 19F NMR spectroscopy Methods 0.000 description 11
- 239000007787 solid Substances 0.000 description 11
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 10
- 239000000203 mixture Substances 0.000 description 10
- 241000894007 species Species 0.000 description 10
- 150000001450 anions Chemical class 0.000 description 9
- OBAJXDYVZBHCGT-UHFFFAOYSA-N tris(pentafluorophenyl)borane Chemical compound FC1=C(F)C(F)=C(F)C(F)=C1B(C=1C(=C(F)C(F)=C(F)C=1F)F)C1=C(F)C(F)=C(F)C(F)=C1F OBAJXDYVZBHCGT-UHFFFAOYSA-N 0.000 description 9
- 239000002904 solvent Substances 0.000 description 8
- 238000004611 spectroscopical analysis Methods 0.000 description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 7
- 150000001768 cations Chemical class 0.000 description 7
- 238000003786 synthesis reaction Methods 0.000 description 7
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- MZRVEZGGRBJDDB-UHFFFAOYSA-N N-Butyllithium Chemical compound [Li]CCCC MZRVEZGGRBJDDB-UHFFFAOYSA-N 0.000 description 6
- 238000010348 incorporation Methods 0.000 description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical class CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 6
- 230000037361 pathway Effects 0.000 description 6
- 238000005481 NMR spectroscopy Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000010936 titanium Substances 0.000 description 5
- 229910052782 aluminium Inorganic materials 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- CPOFMOWDMVWCLF-UHFFFAOYSA-N methyl(oxo)alumane Chemical compound C[Al]=O CPOFMOWDMVWCLF-UHFFFAOYSA-N 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- QFGALIZFMJDZQJ-UHFFFAOYSA-N styrene;toluene Chemical compound CC1=CC=CC=C1.C=CC1=CC=CC=C1 QFGALIZFMJDZQJ-UHFFFAOYSA-N 0.000 description 4
- 229910052719 titanium Inorganic materials 0.000 description 4
- 229910052723 transition metal Inorganic materials 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 0 CC*CC Chemical compound CC*CC 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 229910052768 actinide Inorganic materials 0.000 description 3
- 238000007334 copolymerization reaction Methods 0.000 description 3
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 3
- 238000011065 in-situ storage Methods 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000001953 recrystallisation Methods 0.000 description 3
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 3
- 210000002966 serum Anatomy 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 150000003624 transition metals Chemical class 0.000 description 3
- XEKTVXADUPBFOA-UHFFFAOYSA-N 1-bromo-2,3,4,5,6-pentafluorobenzene Chemical compound FC1=C(F)C(F)=C(Br)C(F)=C1F XEKTVXADUPBFOA-UHFFFAOYSA-N 0.000 description 2
- YXLIKDGPYMCPCT-UHFFFAOYSA-N 1-bromo-2,3,4,5-tetrafluoro-6-(2,3,4,5,6-pentafluorophenyl)benzene Chemical group FC1=C(F)C(F)=C(F)C(F)=C1C1=C(F)C(F)=C(F)C(F)=C1Br YXLIKDGPYMCPCT-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 150000001255 actinides Chemical class 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- ZMMRKRFMSDTOLV-UHFFFAOYSA-N cyclopenta-1,3-diene zirconium Chemical compound [Zr].C1C=CC=C1.C1C=CC=C1 ZMMRKRFMSDTOLV-UHFFFAOYSA-N 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000003760 magnetic stirring Methods 0.000 description 2
- 230000037048 polymerization activity Effects 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- AQZWEFBJYQSQEH-UHFFFAOYSA-N 2-methyloxaluminane Chemical compound C[Al]1CCCCO1 AQZWEFBJYQSQEH-UHFFFAOYSA-N 0.000 description 1
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N C Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- UAEPNZWRGJTJPN-UHFFFAOYSA-N CC1CCCCC1 Chemical compound CC1CCCCC1 UAEPNZWRGJTJPN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 238000010499 C–H functionalization reaction Methods 0.000 description 1
- 241000282326 Felis catus Species 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 229910007926 ZrCl Inorganic materials 0.000 description 1
- HJBREVUYRRNQBW-UHFFFAOYSA-N [HH].[H]C[H]C[H] Chemical compound [HH].[H]C[H]C[H] HJBREVUYRRNQBW-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 125000006267 biphenyl group Chemical group 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000012230 colorless oil Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000013479 data entry Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 238000006471 dimerization reaction Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000002649 leather substitute Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001404 mediated effect Effects 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000012968 metallocene catalyst Substances 0.000 description 1
- 229910052752 metalloid Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000006384 oligomerization reaction Methods 0.000 description 1
- 125000001181 organosilyl group Chemical group [SiH3]* 0.000 description 1
- WYURNTSHIVDZCO-SVYQBANQSA-N oxolane-d8 Chemical compound [2H]C1([2H])OC([2H])([2H])C([2H])([2H])C1([2H])[2H] WYURNTSHIVDZCO-SVYQBANQSA-N 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 229920002725 thermoplastic elastomer Polymers 0.000 description 1
- 238000002061 vacuum sublimation Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/04—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers only
- C08G65/06—Cyclic ethers having no atoms other than carbon and hydrogen outside the ring
- C08G65/16—Cyclic ethers having four or more ring atoms
- C08G65/20—Tetrahydrofuran
-
- 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
- B01J31/146—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 boron
-
- 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
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F17/00—Metallocenes
-
- 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
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/04—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers only
- C08G65/06—Cyclic ethers having no atoms other than carbon and hydrogen outside the ring
- C08G65/08—Saturated oxiranes
- C08G65/10—Saturated oxiranes characterised by the catalysts used
- C08G65/12—Saturated oxiranes characterised by the catalysts used containing organo-metallic compounds or metal hydrides
-
- 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
- B01J2531/30—Complexes comprising metals of Group III (IIIA or IIIB) as the central metal
- B01J2531/39—Actinides
-
- 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
- B01J2531/46—Titanium
-
- 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
-
- 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
- B01J31/1608—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes the ligands containing silicon
-
- 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
- C08F4/619—Component covered by group C08F4/60 containing a transition metal-carbon bond
- C08F4/61908—Component covered by group C08F4/60 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
- C08F4/6592—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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/943—Polymerization with metallocene catalysts
Definitions
- This invention relates to the compositions of matter useful as catalysts, to a method for preparing these catalysts and to a method for polymerization utilizing the catalysts.
- soluble Ziegler-Natta type catalysts in the polymerization of olefins is well known in the prior art.
- such systems include a Group IV-B metal compound and a metal or metalloid alkyl cocatalyst, such as aluminum alkyl cocatalyst. More broadly, it may be said to include a mixture of a Group I-III metal alkyl and a transition metal complex from Group IVB-VB metals, particularly titanium, zirconium, or hafnium with aluminum alkyl cocatalysts.
- the third generation of cocatalyst, B(C 6 F 5 ) 3 proves to be far more efficient while utilizing a 1:1 catalyst-cocatalyst ratio.
- active catalyst species generated with B(C 6 F 5 ) 3 are isolable and characterizable, the anion MeB(C 6 F 5 ) 3 ⁇ , formed after Me ⁇ abstraction from metallocene dimethyl complexes is weakly coordinated to the electron-deficient metal center, thus resulting in a drop of certain catalytic activities.
- a further object of the subject invention is a catalyst which permits better control over molecular weight, molecular distribution, stereoselectivity, and comonomer incorporation.
- Another object of the subject invention is a Ziegler-Natta type catalyst system which reduces the use of excess cocatalyst and activates previously unresponsive metallocenes.
- a strong organo-Lewis acid such as perfluorobiphenylborane (PBB) is utilized as a highly efficient cocatalyst for metallocene-mediated olefin polymerization and as a catalyst for a ring opening polymerization of THF.
- PBB perfluorobiphenylborane
- the anion generated with PBB is non-coordinating instead of weakly coordinating as in the case of B(C 6 F 5 ) 3 .
- the former exhibits higher catalytic activities and can activate previously unresponsive metallocenes.
- the catalytically active species generated with PBB are isolable, X-ray crystallographically characterizable instead of the unstable, oily residues often resulting in the case of B(C 6 F 5 ) 4 ⁇ .
- PBB exhibits even higher catalytic activities in most cases.
- a strong organo-Lewis acid such as perfluorobiphenylborane (PBB)
- PBB perfluorobiphenylborane
- the biphenyl groups of PBB may be connected to the boron at the meta, para, or ortho position.
- PBB reacts with early transition metal or actinide alkyls to yield highly reactive cationic complexes: (CpCp′MR) ⁇ (RBR′R′′ 2 ) ⁇
- CpCp′ C 5 H n R 5-n (n is 0-5), indenyl, allyl, benzyl, C 5 H n R 4-n XNR (n is 0-4);
- M early transition metal or actinide, e.g., Ti, Zr, Hf, Th, U;
- X R′′′ 2 Si, where R′′′ is an alkyl or aryl group (C ⁇ 10);
- R, R′′′ alkyl, benzyl, or aryl group (C ⁇ 20), hydride, silyl;
- R′ fluorinated biphenyl
- R′′ fluorinated phenyl, fluorinated biphenyl, or fluorinated polycyclic fused rings such as naphthyl, anthracenyl, or fluorenyl.
- Such catalytic complexes have been found to be active homogeneous catalysts for ⁇ -olefin polymerization and, more particularly, the polymerization, copolymerization or oligopolymerization of ethylene, ⁇ -olefins, dienes and acetylenic monomers, as well as intramolecular C—H activation.
- FIG. 1 is a structural depiction of PBB
- FIG. 2 is a reaction pathway for the synthesis of PBB
- FIG. 3 shows the reaction pathway for a catalyst system according to the subject invention
- FIG. 4 shows the reaction pathway for a second catalyst system according to the subject invention
- FIG. 5 shows the reaction pathway for a third catalyst system according to the subject invention
- FIG. 6 shows the reaction pathway for a fourth catalyst system according to the subject invention.
- FIG. 7 shows the reaction pathway for a fifth catalyst system according to the subject invention.
- PBB (FIG. 1) has been synthesized in quantitative yields of 91% as compared to the 30-50% yields experienced with B(C 6 F 5 ) 3 , currently a very important Lewis acidic cocatalyst in industry (FIG. 2).
- the former reagent does not effect Me ⁇ abstraction, while the latter gives the catalyst shown in FIG. 3.
- the reaction of PBB with a bis-Cp type of dimethyl zirconocenes forms a dinuclear methyl-bridged zirconocene cation such as
- cationic metallocene catalyst systems can also be created with PBB.
- Metallocene cations of mono-Cp type (FIGS. 4 and 5) have been formed by the reaction of mono-pentamethyl Cp trimethyl group IV complexes with PBB. These are very good syndiospecific styrene polymerization catalysts.
- n-Butyllithium (1.6 M in hexanes, 25 mL, 40 mmol) was added dropwise to bromopentafluorobenzene 18.0 g, 9.1 mL, 72.9 mmol) in 100 mL of diethyl ether over a cold-water bath. The mixture was then stirred for a further 12 h at room temperature. Removal of solvent followed by vacuum sublimation at 60-65° C./10 ⁇ 4 torr gave 12.0 g of 2-bromononafluorobiphenyl as a white crystalline solid: yield 83.3%.
- C 6 F 5 Li-ether solutions in this preparation can be avoided by (a) the use of excess of C 6 F 5 Br, (b) slow addition of n-butyllithium, (c) frequent change of the cold water bath, or use of a continuous flowing cold water bath.
- M Ti.
- the catalyst product of FIG. 5 was generated in the NMR tube reaction by mixing C 5 Me 5 TiMe 3 and PBB at 1:1 molar ratio in C 6 D 6 for2h.
- M Zr. Me 2 Si( t BuN)(C 5 Me 4 )MMe 2 (0.199 mmol) and PBB (0.199 mmol) were treated in the same manner as in the preparation of Example 2 except for the different reaction times (2 h). This procedure yields 73.1 % (yellow solid).
- Analytical and spectroscopic data are as follows.
- the reaction was conducted in a 250 mL flamed round bottom flask attached to a high vacuum line.
- the flask was equipped with a large magnetic stirring bar and a straight-bore high vacuum stopcock.
- the exterior connecting tube of the stopcock (Ca. 10 mm in length) is sealed with a new serum cap.
- the reaction vessel is then evacuated for several hours, back-filled with inert gas (Ar), the stopcock closed, and the reaction flask reevacuated.
- a measured amount of a nonpolar solvent such as benzene or toluene is vacuum transferred into the flask.
- Gaseous ethylene is admitted to the reaction flask through the purification column. The gas pressure is continuously maintained at 1 atm.
- Rapid stirring of the solution is initiated and after several minutes (to allow the saturation of the solvent with ethylene), the stopcock is opened and a small aliquot of catalyst solution (in the same solvent as used for the reaction) is injected by a gas-tight syringe just above the rapidly stirring solution through a serum cap (the syringe needle had been flattened so that the catalyst solution exits in a fine spray).
- Solid polyethylene is formed immediately.
- the reaction is quenched after a certain amount of time by injecting methanol through the serum cap on the stopcock.
- the solid polyethylene was collected by filtration, washed with methanol and then dried under vacuum at 100° C. Copolymerization may occur with the addition of a second monomer such as another ⁇ -olefin.
- Ethylene polymerizations were carried out at room temperature in 250-mL flamed, round-bottom flasks attached to a high-vacuum line.
- a solution of each of the catalysts of Example 3 in 2 mL of toluene was quickly injected using a gas-tight syringe equipped with a spraying needle into respective rapidly stirred flasks containing 100 mL of toluene which was pre-saturated under 1 atm of rigorously purified ethylene.
- the catalyst solution was generated in situ by mixing Cp 2 ZrMe 2 and PBB in 2 mL of toluene after aging for 0.5 h at 60° C., and then quickly injected into respective flasks under an ethylene atmosphere using a pre-warmed gas-tight syringe.
- the polymerization was quenched with acidic CH 3 OH after a short time period (10-60 s) at which point voluminous quantities of polyethylene precipitated out.
- the respective polymeric products were collected by filtration, washed with methanol and dried under high vacuum to a constant weight.
- This reaction is carried out in a 100 mL quartz Worden vessel equipped with a magnetic stirring bar, a pressure gauge and a stainless steel o-ring assembly attached to a high vacuum line.
- the reaction vessel is flamed and then pumped under high vacuum for several hours, filled with inert gas and brought into a glove box.
- a measured amount of catalyst is added into the vessel.
- On the high vacuum line, a measured amount of the solvent and propylene are condensed in at ⁇ 78 ° C.
- the reaction apparatus is sealed off and warmed to the desired temperature.
- the reaction tube is immersed in a large amount of tap water (20-25° C.) or ice water (0° C.) to help dissipate the heat produced from the polymerization and keep the temperature constant.
- the progress of the polymerization reactions is monitored through observance of the pressure change.
- the reaction is finished (pressure drops to zero psi)
- the resulting oily liquid is removed from the vessel, washed with methanol and water and dried under vacuum at 90-100° C. for ten hours to result in a colorless oil.
- Table II sets forth the relevant data concerning propylene polymerization utilizing the catalyst prepared according to the enumerated example.
- Example 3 5 Metallocene (Cp 2 ZrMe) 2 Me ⁇ / (Cp 2 ZrMe ⁇ )/ Cation/Anion* (MePBB) ⁇ (MePBB) ⁇ Catalyst (mM) 0.15 0.15 Reaction Time (m) 40 40 Yield (g) 4.0 5.0
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
Description
- This application is a division of prior copending application Ser. No. 09/329,431, filed Jun. 10, 1999, which is a continuation-in-part of application Ser. No.09/220,741, filed Dec. 23, 1998, now U.S. Pat. No. 6,087,460, issued Jul. 11, 2000, which is a division of application Ser. No. 08/800,548, filed Feb. 18, 1997, now U.S. Pat. No. 5,856,256, issued Jan. 5, 1999, which in turn claims priority of U.S. provisional application Ser. No.60/011,920, filed Feb. 20, 1996.
- [0002] This invention was made with Government support under Contract No. DE-FG02-86ER13511 awarded by the Department of Energy. The Government has certain rights in this invention.
- This invention relates to the compositions of matter useful as catalysts, to a method for preparing these catalysts and to a method for polymerization utilizing the catalysts.
- The use of soluble Ziegler-Natta type catalysts in the polymerization of olefins is well known in the prior art. In general, such systems include a Group IV-B metal compound and a metal or metalloid alkyl cocatalyst, such as aluminum alkyl cocatalyst. More broadly, it may be said to include a mixture of a Group I-III metal alkyl and a transition metal complex from Group IVB-VB metals, particularly titanium, zirconium, or hafnium with aluminum alkyl cocatalysts.
- First generation cocatalyst systems for homogeneous metallocene Ziegler-Natta olefin polymerization, alkylaluminum chlorides (AlR 2Cl), exhibit low ethylene polymerization activity levels and no propylene polymerization activity. Second generation cocatalyst systems, utilizing methyl aluminoxane (MAO), raise activities by several orders of magnitude. In practice however, a large stoichiometric excess of MAO over catalyst ranging from several hundred to ten thousand must be employed to have good activities and stereoselectivities. Moreover, it has not been possible to isolate characterizable metallocene active species using MAO. The third generation of cocatalyst, B(C6F5)3, proves to be far more efficient while utilizing a 1:1 catalyst-cocatalyst ratio. Although active catalyst species generated with B(C6F5)3, are isolable and characterizable, the anion MeB(C6F5)3 ⊖, formed after Me⊖ abstraction from metallocene dimethyl complexes is weakly coordinated to the electron-deficient metal center, thus resulting in a drop of certain catalytic activities. The recently developed B(C6F5)4 ⊖ type of non-coordinating anion exhibits some of the highest reported catalytic activities, but such catalysts have proven difficult to obtain in the pure state due to poor thermal stability and poor crystallizability, which is crucial for long-lived catalysts and for understanding the role of true catalytic species in the catalysis for the future catalyst design. Synthetically, it also takes two more steps to prepare such an anion than for the neutral organo-Lewis acid.
- Accordingly, it is an object of the subject invention to prepare and utilize a new class of olefin polymerization catalysts.
- A further object of the subject invention is a catalyst which permits better control over molecular weight, molecular distribution, stereoselectivity, and comonomer incorporation.
- Another object of the subject invention is a Ziegler-Natta type catalyst system which reduces the use of excess cocatalyst and activates previously unresponsive metallocenes.
- These and other objects are attained by the subject invention whereby in one embodiment, a strong organo-Lewis acid, such as perfluorobiphenylborane (PBB) is utilized as a highly efficient cocatalyst for metallocene-mediated olefin polymerization and as a catalyst for a ring opening polymerization of THF. PBB can be synthesized in much higher yield than B(C 6F5)3 and the anion generated with PBB is non-coordinating instead of weakly coordinating as in the case of B(C6F5)3. Thus, the former exhibits higher catalytic activities and can activate previously unresponsive metallocenes. The catalytically active species generated with PBB are isolable, X-ray crystallographically characterizable instead of the unstable, oily residues often resulting in the case of B(C6F5)4 ⊖. In addition, PBB exhibits even higher catalytic activities in most cases.
- In one embodiment of the subject invention a strong organo-Lewis acid, such as perfluorobiphenylborane (PBB), is utilized to synthesize stoichiometrically precise, isolable/crystallographically characterizable, highly active “cation-like” metallocene polymerization catalysts. The biphenyl groups of PBB may be connected to the boron at the meta, para, or ortho position.
- PBB reacts with early transition metal or actinide alkyls to yield highly reactive cationic complexes: (CpCp′MR) ⊕(RBR′R″2)⊖
- where
- CpCp′=C 5HnR5-n(n is 0-5), indenyl, allyl, benzyl, C5HnR4-nXNR (n is 0-4);
- M=early transition metal or actinide, e.g., Ti, Zr, Hf, Th, U;
- X=R′″ 2Si, where R′″ is an alkyl or aryl group (C≦10);
- R, R′″=alkyl, benzyl, or aryl group (C≦20), hydride, silyl;
- B=boron
- R′=fluorinated biphenyl
- R″=fluorinated phenyl, fluorinated biphenyl, or fluorinated polycyclic fused rings such as naphthyl, anthracenyl, or fluorenyl.
-
- Such catalytic complexes have been found to be active homogeneous catalysts for α-olefin polymerization and, more particularly, the polymerization, copolymerization or oligopolymerization of ethylene, α-olefins, dienes and acetylenic monomers, as well as intramolecular C—H activation.
- The cocatalyst of the subject invention may be referred to as BR′R″ 2, where B=boron; R′ and R″ represent at least one and maybe more fluorinated biphenyls or other polycyclic groups, such as naphthyl. Two of the biphenyls may be substituted with a phenyl group. Both the biphenyls and the phenyl groups should be highly fluorinated, preferably with only one or two hydrogens on a group, and most preferably, as in PBB with no hydrogens and all fluorines.
- The cocatalyst system of the subject invention can be better understood with reference to the drawings wherein:
- FIG. 1 is a structural depiction of PBB;
- FIG. 2 is a reaction pathway for the synthesis of PBB;
- FIG. 3 shows the reaction pathway for a catalyst system according to the subject invention;
- FIG. 4 shows the reaction pathway for a second catalyst system according to the subject invention;
- FIG. 5 shows the reaction pathway for a third catalyst system according to the subject invention;
- FIG. 6 shows the reaction pathway for a fourth catalyst system according to the subject invention; and
- FIG. 7 shows the reaction pathway for a fifth catalyst system according to the subject invention.
- The reaction of perfluorobiphenylborane with a variety of zirconocene and other actinide or transition metal dimethyl complexes proceeds rapidly and quantitatively at room temperature in noncoordinating solvents to yield, after recrystallization, complexes. This catalyst activation reaction may be used in the polymerization, copolymerization, oligomerization and dimerization of α-olefins. In addition, the catalyst of the subject invention may be used in conjunction with aluminum alkyls, aluminum aryls, (AlR 3, R=Et, Me, Ph, naphthyl) or methyl alumoxane (Al(CH3)O)n for increased polymer yields.
- PBB (FIG. 1) has been synthesized in quantitative yields of 91% as compared to the 30-50% yields experienced with B(C 6F5)3, currently a very important Lewis acidic cocatalyst in industry (FIG. 2). The Lewis acidity of PBB has been shown to be much greater than that of B(C6F5)3 by comparative reactions of Cp*2ThMe2 with B(C6F5)3 and PBB (Cp*=C5Me5). The former reagent does not effect Me⊖ abstraction, while the latter gives the catalyst shown in FIG. 3. The reaction of PBB with a bis-Cp type of dimethyl zirconocenes forms a dinuclear methyl-bridged zirconocene cation such as
- (1:1 or 2:1)
- where
- Cp=C 5H5
- Cp=C 5H3Me2 or
- Cp=C 5Me5
-
- where
- Cp=C 5H5 or
- Cp=C 5H3Me2
- More particularly, reaction of PBB with
group 4 and Th methyls proceeds cleanly to yield cationic complexes such as set forth below.Cp = η5-C5 H 51, Cp*2ThMe⊕[MePBB]⊖ Cp* = η5-Me5 C 52, Cp2ZrCl⊕[MePBB]⊖ Cp″ = η5-1,2-Me2C5H3 3, [Cp2ZrMe(μ-Me)MeZrCp2]⊕[MePBB]⊖ CGC = (Me4C5)SiMe2NtBu 4, [Cp″2ZrMe(μ-Me)MeZrCp″2]⊕[MePBB]⊖ M = Th, Zr, Hf, Ti 5, [Cp2*ZrMe(μ-Me)MeZrCp2*]⊕[MePBB]⊖ 6, [(Me4C5)SiMe2NtBu]ZrMe⊕[MePBB]⊖ 7, [(Me4C5)SiMe2NtBu]TiMe⊕[MePBB]⊖ 8, Cp*ZrMe2 ⊕[MePBB]⊖ 9, Cp*HfMe2 ⊕[MePBB]⊖ - For ethylene polymerization, catalytic activities of dinuclear cations generated from PBB are greater than those of monomeric cations generated from B(C 6F5)3 presumably because (MePBB)⊖ is a non-coordinating anion as compared to the weakly coordinating anion MeB(C6F5)3. The dinuclear cations have also been found to catalyze the rapid ring-opening polymerization of THF to produce poly(tetrahydrofuran), an important thermoplastic elastomer and artificial leather. Monomeric zirconocene cations have also been generated in situ by the reaction of Cp2ZrMe2 and PBB at 60° C.:
- These attempts show very high activities for olefin polymerization, and identify (MePBB) ⊖ to be a truly non-coordinating anion. The polymerization data with metallocene cations having various anions are summarized in Table 1.
TABLE 1 Polymerization Data Entry μmol Polymer Mwd c No. Catalyst of cat Conditions Monomer(s)a yield (g) Activityb (10−3) Mw/Mn Remarks 1 (Cp2ZrMe)2Me⊕ 15 100 mL toluene ethylene 0.80 4.80 × 106 559 3.06 MePBB⊖ 25° C., 40 s 2 Cp2ZrMe⊕ 15 100 mL toluene ethylene 1.00 4.00 × 106 124 2.03 MeB(C6F5)3 ⊖ 25° C., 60 s 3 (Cp″2ZrMe)2Me⊕ 15 100 mL toluene ethylene 1.30 7.80 × 106 392 2.72 MePBB⊖ 25° C., 40s 4 Cp″2ZrMe⊕ 15 100 mL toluene ethylene 1.50 6.00 × 106 321 1.42 MeB(C6F5)3 ⊖ 25° C., 60 s 5 (Cp*2ZrMe)2Me⊕ 15 100 mL toluene ethylene 1.07 4.30 × 106 370 2.28 MePBB⊖ 25° C., 60 s 6 Cp*2ZrMe⊕ 15 100 mL toluene ethylene 0.80 3.20 × 106 136 2.54 MeB(C6F5)3 ⊖ 25° C., 60 s 7 Cp*TiMe⊕ 2 50 5 mL toluene styrene 0.35 1.61 × 106 170 2.56 [rrrr] > 98% MePBB⊖ 25° C., 15 min 8 Cp*ZrMe⊕ 2 50 5 mL toluene styrene 1.45 1.00 × 107 27.6 2.63 atactic MePBB⊖ 25° C., 10 min 9 Cp*HfMe⊕ 2 50 5 mL toluene styrene 0.69 3.17 × 106 24.8 2.98 atactic MeB(C6F)3 ⊖ 25° C., 15 min 10 Cp*HfMe⊕ 2 50 5 mL toluene styrene 1.16 5.33 × 106 22.9 2.78 atactic MePBB⊖ 25° C., 15 min 11 Cp*TiMe⊕ 2 50 25 mL toluene ethylene 0.70 1.70 × 105 848 23.7 39.5% hexene MeB(C6F5)3 ⊖ 25° C., 5 min 1-hexene incorporation 12 Cp*TiMe⊕ 2 50 25 mL toluene ethylene 4.51 1.08 × 106 151 4.32 43.6% hexene MePBB⊖ 25° C., 5 min 1-hexene incorporation 13 CGCZrMe⊕ 15 100 mL toluene ethylene 0 — — — MeB(C6F5)3 ⊖ 25° C., 20 min 14 CGCZrMe⊕ 15 100 mL toluene ethylene 1.56 1.56 × 106 7.69 2.78 MePBB⊖ 25° C., 4 min 15 CGCTiMe⊕ 15 100 mL toluene ethylene 0.21 8.40 × 104 1058 9.54 MeB(C6F5)3 ⊖ 25° C., 10 min 16 CGCTiMe⊕ 15 100 mL toluene ethylene 0.83 4.98 × 106 305 2.56 MePBB⊖ 25° C., 40 s 17 CGCZrMe⊕ 50 25 mL toluene ethylene 0 — — — MeB(C6F5)3 ⊖ 25° C., 15 min 1-hexene 18 CGCZrMe⊕ 50 25 mL toluene ethylene 6.97 5.58 × 105 10.0 2.68 33.6% hexene MePBB⊖ 25° C., 15 min 1-hexene incorporation 19 CGCTiMe⊕ 25 25 mL toluene ethylene 0.05 1.20 × 104 63.2% hexene MeB(C6F5)3 ⊖ 25° C., 10 min 1-hexene incorporation 20 CGCTiMe⊕ 25 25 mL toluene ethylene 1.95 4.68 × 105 105 1.86 65.3% hexene MePBB⊖ 25° C., 10 min 1-hexene incorporation - Other types of cationic metallocene catalyst systems can also be created with PBB. Metallocene cations of mono-Cp type (FIGS. 4 and 5) have been formed by the reaction of mono-pentamethyl Cp trimethyl group IV complexes with PBB. These are very good syndiospecific styrene polymerization catalysts. Constrained geometry types of zirconocene and titanocene cations such as those in FIG. 6 where m=Zr, Ti, are readily produced by the reaction of the corresponding dimethyl metallocenes with PBB. They are highly naked cations and much more active catalysts than those generated with B(C 6F5)3.
- n-Butyllithium (1.6 M in hexanes, 25 mL, 40 mmol) was added dropwise to bromopentafluorobenzene 18.0 g, 9.1 mL, 72.9 mmol) in 100 mL of diethyl ether over a cold-water bath. The mixture was then stirred for a further 12 h at room temperature. Removal of solvent followed by vacuum sublimation at 60-65° C./10 −4 torr gave 12.0 g of 2-bromononafluorobiphenyl as a white crystalline solid: yield 83.3%. The dangerous and explosive nature of C6F5Li-ether solutions in this preparation can be avoided by (a) the use of excess of C6F5Br, (b) slow addition of n-butyllithium, (c) frequent change of the cold water bath, or use of a continuous flowing cold water bath.
- To the above prepared 2-bromononafluorobiphenyl (5.0 g, 12.7 mmol) in a mixed solvent of 70 mL of diethyl ether and 70 mL of pentane was gradually added 8.0 mL of n-butyllithium (1.6 M in hexanes, 12.8 mmol) at −78° C. The mixture was stirred for an additional 2 h, and boron trichloride (4.0 mL, 1.0 M in hexanes, 4.0 mmol) was then quickly added by a syringe. The mixture was left at −78° C. for 1 h and the temperature was then allowed to slowly rise to room temperature. A suspension resulted after stirring an additional 12 h. It was filtered to give a yellow solution, and the solvent of the filtrate was removed in vacuo. The resulting pale yellow powder was sublimed at 140° C./10 −4 torr or 125° C./10−6 torr to produce a light yellow crystalline solid as an ether-free crude product. Recrystallization from pentane at −20° C. gave 3.5 g of the pure PBB as a white crystalline solid: yield 91.0%. Analytical and spectroscopic data for PBB are as follows. 19F NMR (C6D6, 23° C.): δ-120.08 (s, br, 3 F, F-3), −132.09 (s, br, 3 F, F-6), −137.66 (s, br, 6 F, F-2′/F-6′), −143.31 (t, 3JF-F=21.4 Hz, 3 F, F-4), −149.19 (t, 3JF-F=21.7 Hz, 3 F. F-4′), −150.56 (t, 3JF-F =14.7 Hz, 3 F, F-5), 160.72 (s, br, 6 F, F-3′/F-5′). 13C NMR(C6D6, 23° C.): δ150.92 (dd, 1JC-F=251.8 Hz, 2JC-F=10.1 Hz, 3 C),146.35 (dd, J C-F=254.3 Hz, 2JC-F=12.1 Hz, 3 C), 144.26 (dd, 1JC-F=258.1 Hz, 2JC-F=10.5 Hz, 6 C), 143.50 (tt, 1JC-F=265.4 Hz, 2JC-F=12.0 Hz, 3 C), 141.98 (tt, 1JC-F=261.4 Hz, 2JC-F=11.7 Hz, 3 C), 141.17 (tt, 1JC-F=254.3 Hz, 2JC-F=10.5 Hz, 3 C), 137.70 (tt, 1JC-F=257.3 Hz, 2JC-F=11.6 Hz, 6 C), 124.51 (d, 2JC-F=11.7 Hz, 3 C), 113.60 (d, 2JC-F=11.5 Hz, 3 C), 106.05 (s, br, 3 C). MS: parent ion at m/e 956. Anal. Calcd for C36BF27: C, 45.22; H, 0.00. Found: C, 45.44; H, 0.05.
- Cp* 2ThMe2 (0.106 g, 0.199 mmol) and PBB (0.191 g, 0.199 mmol) were in the glove box charged into a 25-mL reaction flask with a filter plug, and the flask was attached to the high vacuum line. Benzene (15 mL) was then vacuum-transferred into this flask at −78° C. The mixture was slowly allowed to warm to room temperature and stirred for 6 h. The solvent was removed, pentane (20 mL) was next vacuum-transferred into the flask, and the mixture was filtered after stirring. The white solid which collected was dried under vacuum to give 0.210 g of product: yield 70.9%. Analytical and spectroscopic data are as follows. 1H NMR (C6D6, 23° C.): δ1.61 (s, 30 H, C5Me5), 0.62 (s, 3 H, Th—CH3), −095 (s, br, 3 H, B—CH3). 19F NMR (C6D6, 23° C.): δ-124.57 (s, br, 3F), −138.10 (s, br, 3 F), −139.28 (d, 3JF-F=21.4 Hz, 3 F), −139.74 (d, 3JF-F=21.2 Hz, 3 F), −155.08 (t, 3JF-F 21.4 Hz, 3 F), −157.32 (t, 3JF-F=22.0 Hz, 3 F), −162.20 (t, 3JF-F=22.0 Hz, 3 F), −163.13 (t, 3JF-F=22.0 Hz, 3 F), −163.90 (t, 3JF-F=21.4 Hz, 3 F). 13C NMR (C6D6, 23° C.): δ129.54 (C5Me5), 79.28 (Th—Me), 10.44 (C5Me5), 10.25 (B—Me). Anal. Calcd for C58 H36 BF27 Th: C, 46.79; H, 2.44; N, 0.00. Found: C, 46.68; H, 2.24; N. 0.00.
- Cp 2ZrMe2 (0.398 mmol) and PBB (0.199 mmol) were loaded into a 25 mL-flask, which was then attached to the vacuum line. Pentane (20 mL) was then vacuum-transferred into this flask at −78 ° C. The mixture was slowly warmed to room temperature and stirred for an additional 2 h (Cp=C5H5), 15 h (Cp=C5H3Me2) or 48 h (Cp=C5Me5). The resulting suspension was filtered, and the colored solids (light pink for C5H5, light yellow for C5H3Me2 and yellow for C5Me5) were washed with a small amount of pentane and dried under vacuum: yields 90.3% (C5H5), 86.3% (C5H3Me2) and 34.7% (C5Me5). Analytical and spectroscopic data for Cp=C5H5 are as follows. 1H NMR (C6D6, 23° C.): δ5.65 (s, 20 H, C5H5), −0.04 (s, 6 H, Zr—CH3), −0.84 (s, br, 3 H, B—CH3), −1.15 (s, 3 H, Zr—CH3—Zr). 19F NMR (C6D6, 23° C.): δ124.20 (d, 3JF-F=16.6 Hz, 3 F), −138.98 (d, 3JF-F=20.3 Hz, 3 F), −139.20 (d, 3JF-F=22.0 Hz, 3 F), −140.29 (d, 3JF-F=24.5 Hz, 3 F), −155.15 (t, 3JF-F=20.9 Hz, 3 F), −160.06 (t, 3JF-F=22.3 Hz, 3 F), −162.79 (t, 3JF-F=22.0 Hz, 3 F), −163.11 (t, 3JF-F=21.5 Hz, 3 F), −163.97 (t, 3JF-F=19.0 H,3 F). 13C NMR(C6D6, 23° C.):δ113.24(C5H5),38.88(Zr—CH3),21.53 (B—CH3), 15.80 (Zr—CH3—Zr). Anal. Calcd for C60H32BF27Zr2: C, 49.39; H, 2.21; N, 0.00. Found: C, 48.97; H, 1.92; N 0.00.
- Analytical and spectroscopic data for Cp=C 5H3Me2 are as follows. 1H NMR (C7D8, 23° C.): 65.51 (t, 3JH-H=2.8 Hz, 4 H, C5H3 Me2), 5.47 (t, 3JH-H=3.2 Hz, 4 H, C5H3Me2), 5.18 (t, 3JH-H=2.8 Hz, 4 H, C5H3Me2).1.73 (s, 12 H, C5H3Me2), 1.51 (s, 12 H, C5H3MMe2), −0.26 (s, 6 H, Zr—CH3), −0.92 (s, br, 3 H, B—CH3), −1.50 (s, 3 H, Zr—CH3—Zr). 19F NMR (C6D6, 23° C.): δ123.37 (d, 3JF-F=15.3 Hz, 3 F), −139.20 (d, 3JF-F=24.0 Hz, 3 F), −139.62 (d, 3JF-F=24.3 Hz, 3 F), −139.89 (d, 3JF-F=24.0 Hz, 3 F), −155.81 (t, 3JF-F=2.14 Hz, 3 F), −159.36 (t, 3JF-F=22.3 Hz, 3 F), −163.22 (t, 3JF-F=21.4 Hz, 3 F), −16.55 (t, 3JF-F=22.0 Hz, 3 F), −164.20 (t, 3JF-F=22.6 Hz, 3 F). 13C NMR (C6D6, 23° C.): δ114.20 (d, 1JCH=17.1 Hz, C5H3Me2), 113.62 (s, C5H3Me2), 112.80 (s, C5H3Me2), 111.29 (d, 1JCH=165.7 Hz, C5H3Me2), 106.57 (d, 1JCH=173.3 Hz. C5H3Me2), 41.63 (q, 1JCH=118.4 Hz, Zr—CH3), 31.26 (q, 1JCH=116.5 Hz, B—CH3), 22.21 (q, 1JCH=134.3 Hz, Zr—CH3—Zr), 12.94 (q, 1JCH=128.0 Hz, C5H2Me2), 12.71 (q, 1JCH=127.6 Hz. C5H2Me2). Anal. Calcd for C68H48BF27Z2: C, 51,98; H, 3.08; N, 0.00. Found: C, 51.61; H, 3.00; N, 0.00.
- Analytical and spectroscopic data for Cp=C 5Me5 are as follows. 1H NMR (C6D6, 23° C.): δ1.57 (s, 60 H, C5Me5) −0.84 (s, br, 3 H, B—CH3). The bridging and terminal methyl groups are discrete at low temperature. 1H NMR (C7D8, 13° C.): δ−0.19 (s, br, 6 H. Zr—CH3), −0.92 (s, br, 3 H, B—CH3), −2.42 (s, br, 3 H, Zr—CH3—Zr). 19F NMR (C6D6, 23° C.): δ−123.11 (d, s, br, 3 F), −139.27 (d, 3JF-F=20.3 Hz, 3 F), −139.67 (t, 3JF-F=25.1 Hz, 6F), −155.73 (t, 3JF-F=20.9 Hz, 3 F), −160.91 (s, br, 3 F), −163.25 (t, 3JF-F=21.7 Hz, 3F), −163.56 (t, 3JF-F=22.0 Hz, 3 F), −164.13 (t, 3JF-F=21.4 Hz, 3 F). Anal. Calcd for C80H72BF27Zr2: C, 55.23; H, 4.17; N, 0.00. Found: C, 54.81; H, 3.98; N, 0.00.
- The procedure here is similar to that of Example 3, except that the reaction was carried out under 1 atm of H 2 for 15 h: yields 81.6% (Cp=C5H5, grey solid) and 75.6% (Cp=C5H3Me2, orange solid). Analytical and spectroscopic data for Cp=C5H5 are as follows. 1H NMR (C6D6, 58° C.): δ6.67 (s, br, 2 H, Zr—H), 5.64 (s, 20 H, C5H5), −0.81 (s, br, 3 H, B—CH3), −1.38 (s, br, 1 H, Zr—H—Zr). The chemical shifts and splitting patterns of 19F NMR are same as those of Example 3 (Cp=C5H5). Anal. Calcd for C57H26BF27Zr2: C, 48.31; H, 1.85; N, 0.00. Found: C, 47.90; H, 1.92; N, 0.00.
- Analytical and spectroscopic data for Cp=C 5H3Me2 are as follows. 1H NMR (C7D8, 23° C.): δ5.81 (m, 4 H, C5H3Me2),5.50 (m,4 H, C5H3Me2),523 (m, 4 H, C5H3Me2). 1.65 (m, 24 H, C5H3Me2), 0.25 (s, br, 2 H, Zr—H), −0.94 (s, br, 3 H, B—CH3), −1.52 (s, br, 1 H, Zr—H—Zr). The chemical shifts and splitting patterns of 19F NMR are same as those of Example 3 (Cp=C5H3Me2). Anal. Calcd for C65H42BF27Zr2: C, 51.05; H, 2.77; N, 0.00. Found C, 51.07; H. −2.63; N. 0.00.
- 5(a) Cp=C 5H5. In a J-Young NMR tube, a small amount of a mixture of Cp2ZrMe2 and PBB (1:1.2 molar ratio) was dissolved in C6D6). The NMR tube was then put in an NMR probe and heated at 60° C. After 0.5 h, 1H NMR revealed the above monomeric species formed. The same structures were obtained by the reaction of the product of Example 3 with excess of PBB at 60° C. for 0.5 h. In a real polymerization test, these species were also generated in situ by mixing Cp2ZrMe2 and PBB at 60° C. for 0.5 h. 1H NMR (C6D6, 60° C.) for: δ5.70 (s, 10 H, C5H5), 0.14 (s, 3 H, Zr—CH3), −0.85 (s, br, 3 H, B—CH3). The 19F NMR is similar to that of the corresponding dinuclear species of Example 3 (Cp=C5H5).
- 5(b) Cp=C 5H3Me2. The same procedure of Example 5(a) was used to prepare this species. In the polymerization test, the following was observed: 1H NMR (C7D8, 60° C.) for 8: δ5.68 (t, 3 J H-H=2.8 Hz, 4 H, C5H3Me2), 5.36 (t, 3JH-H=3.1 Hz, 4 H, C5H3Me2), 5.23 (t, 3JH-H=2.8 Hz, 4 H, C5H3Me2).1.76 (s, 6 H, C5H3Me2), 1.56 (s, 6 H, C5H3Me2), 0.17 (s, 3 H, Zr—CH3), −0.93 (s, br, 3 H, B—CH3). 19F NMR of this species is similar to that of the corresponding dinuclear species of Example 3 (Cp=C5Me5). 13C NMR (C7D8, 60° C.): δ117.74 (C5H3Me2), 112.14 (C5H3Me2), 108.01 (C5H3Me2), 42.11 (Zr—CH3), 34.43 (B—CH3), 12.63 (C5H2Me2), 12.45 (C5H2Me2).
- (c) Cp=C 5Me5 The same procedure of Example 5 (a) was used to prepare this species. In the polymerization test, the following was observed: 1H NMR (C6D6, 60° C.): δ1.61 (s, 30 H, C5Me5), 0.13 (s, 3 H, Zi—CH3), −0.86 (s, br, 3 H, B—CH3). 19F NMR is similar to that of the corresponding dinuclear species of Example 3, Cp=C5Me5.
- M=Ti. The catalyst product of FIG. 5 was generated in the NMR tube reaction by mixing C 5Me5TiMe3 and PBB at 1:1 molar ratio in C6D6for2h. 1H NMR(C6D6, 23° C.): δ9.03 (s, br, 2 H. CH2), 1.69 (s, 6 H, C5Me4), 1.65 (s, 6 H, C5Me4), 0.15 (s, 3 H, Ti—CH3), −0.82 (s, br, 3 H, B—CH3).
- M=Zr. Me 2Si(tBuN)(C5Me4)MMe2 (0.199 mmol) and PBB (0.199 mmol) were treated in the same manner as in the preparation of Example 2 except for the different reaction times (2 h). This procedure yields 73.1 % (yellow solid). Analytical and spectroscopic data are as follows. 1H NMR (C7D8, 23 ° C.): δ1.73 (s, 3 H, C5Me4), 1.69 (s, 3 H, (C5Me4), 1.63 (s, 3 H, C5Me4), 1.43 (s, 3 H, C5Me4), 0.85 (s, 9 H, N-tBu), 0.28 (s, 3 H, SiMe2), 0.21 (s, 3 H, SiMe2), −0.48 (s, 3 H, Zr—CH3), −0.95 (s, br, 3 H, B—CH3). 19F NMR (C7D8, 23° C.): δ124.20 (s, br, 3 F), −139.14 (d, 3JF-F=23.7 Hz, 3 F), −139.35 (d, 3JF-F=22.0 Hz, 3 F), −139.93 (d, 3JF-F=21.2 Hz, 3 F), −155.79 (t, 3JF-F=21.2 Hz, 3 F), −159.67 (t, 3JF-F=22.3 Hz, 3 F), −163.28 (t, 3JF-F=21.7 Hz, 3 F), −163.87 (t, 3JF-F=22.6 Hz, 3 F), −164.13 (t, 3JF-F=22.6 Hz, 3 F). 13C NMR (C7D8, 23° C.): δ130.22 (C5Me4), 128.18 (C5Me4), 127.22 (C5Me4), 126.47 (C5Me4), 124.37 (C5Me4), 58.47 (N—CMe3), 34.37 (Zr—CH3), 34.10 (N—CMe3), 15.89 (C5Me4), 13.46 (C5Me4), 11.77 (C5Me4), 10.99 (C5Me4), 7.92 (SiMe2), 5.65 (SiMe2). Anal. Calcd for C53H33BF27NSiZr: C, 47.97; H, 2.51; N, 1.06, Found: C, 47.79; H, 2.58; N, 0.86.
- The reaction was conducted in a 250 mL flamed round bottom flask attached to a high vacuum line. The flask was equipped with a large magnetic stirring bar and a straight-bore high vacuum stopcock. The exterior connecting tube of the stopcock (Ca. 10 mm in length) is sealed with a new serum cap. The reaction vessel is then evacuated for several hours, back-filled with inert gas (Ar), the stopcock closed, and the reaction flask reevacuated. A measured amount of a nonpolar solvent such as benzene or toluene is vacuum transferred into the flask. Gaseous ethylene is admitted to the reaction flask through the purification column. The gas pressure is continuously maintained at 1 atm. Rapid stirring of the solution is initiated and after several minutes (to allow the saturation of the solvent with ethylene), the stopcock is opened and a small aliquot of catalyst solution (in the same solvent as used for the reaction) is injected by a gas-tight syringe just above the rapidly stirring solution through a serum cap (the syringe needle had been flattened so that the catalyst solution exits in a fine spray). Solid polyethylene is formed immediately. The reaction is quenched after a certain amount of time by injecting methanol through the serum cap on the stopcock. The solid polyethylene was collected by filtration, washed with methanol and then dried under vacuum at 100° C. Copolymerization may occur with the addition of a second monomer such as another α-olefin.
- Ethylene polymerizations were carried out at room temperature in 250-mL flamed, round-bottom flasks attached to a high-vacuum line. In a typical experiment, a solution of each of the catalysts of Example 3 in 2 mL of toluene was quickly injected using a gas-tight syringe equipped with a spraying needle into respective rapidly stirred flasks containing 100 mL of toluene which was pre-saturated under 1 atm of rigorously purified ethylene. In the case of the catalysts prepared in Example 3, the catalyst solution was generated in situ by mixing Cp 2ZrMe2 and PBB in 2 mL of toluene after aging for 0.5 h at 60° C., and then quickly injected into respective flasks under an ethylene atmosphere using a pre-warmed gas-tight syringe. The polymerization was quenched with acidic CH3OH after a short time period (10-60 s) at which point voluminous quantities of polyethylene precipitated out. The respective polymeric products were collected by filtration, washed with methanol and dried under high vacuum to a constant weight.
- A small amount of [(C 5H3Me2)2(Me)Zr—Me—Zr(Me)(C5H3Me2)2]⊕(MePBB)⊖ was loaded into a J-Young NMR tube and THF-d8 was then vacuum-transferred into the tube. The mixture was slowly warmed to room temperature and left for several hours. The solid polymer formed in the tube was shown to be polytetrahydrofuran by 1H analysis.
- This reaction is carried out in a 100 mL quartz Worden vessel equipped with a magnetic stirring bar, a pressure gauge and a stainless steel o-ring assembly attached to a high vacuum line. In a typical experiment, the reaction vessel is flamed and then pumped under high vacuum for several hours, filled with inert gas and brought into a glove box. A measured amount of catalyst is added into the vessel. On the high vacuum line, a measured amount of the solvent and propylene are condensed in at −78 ° C. The reaction apparatus is sealed off and warmed to the desired temperature. During the polymerization process, the reaction tube is immersed in a large amount of tap water (20-25° C.) or ice water (0° C.) to help dissipate the heat produced from the polymerization and keep the temperature constant. The progress of the polymerization reactions is monitored through observance of the pressure change. After the reaction is finished (pressure drops to zero psi), the resulting oily liquid is removed from the vessel, washed with methanol and water and dried under vacuum at 90-100° C. for ten hours to result in a colorless oil.
- Table II sets forth the relevant data concerning propylene polymerization utilizing the catalyst prepared according to the enumerated example.
TABLE II Example 3 5 Metallocene (Cp2ZrMe)2Me⊕/ (Cp2ZrMe⊕)/ Cation/Anion* (MePBB)⊖ (MePBB)⊖ Catalyst (mM) 0.15 0.15 Reaction Time (m) 40 40 Yield (g) 4.0 5.0 - While the invention has been described with reference to a preferred embodiment, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this invention, but that the invention will include all embodiments and equivalents falling within the scope of the appended claims.
- Various features of the invention are set forth in the following claims.
Claims (79)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/899,698 US6403733B2 (en) | 1996-02-20 | 2001-07-05 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US1192096P | 1996-02-20 | 1996-02-20 | |
| US08/800,548 US5856256A (en) | 1996-02-20 | 1997-02-18 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
| US09/220,741 US6087460A (en) | 1996-02-20 | 1998-12-23 | Organo-Lewis acid as cocatalyst for cationic homogenous metallocene Ziegler-Natta olefin polymerizations |
| US09/329,431 US6274752B1 (en) | 1996-02-20 | 1999-06-10 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
| US09/899,698 US6403733B2 (en) | 1996-02-20 | 2001-07-05 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/329,431 Division US6274752B1 (en) | 1996-02-20 | 1999-06-10 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| US20020010080A1 true US20020010080A1 (en) | 2002-01-24 |
| US6403733B2 US6403733B2 (en) | 2002-06-11 |
Family
ID=27359530
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/329,431 Expired - Lifetime US6274752B1 (en) | 1996-02-20 | 1999-06-10 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
| US09/899,698 Expired - Lifetime US6403733B2 (en) | 1996-02-20 | 2001-07-05 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US09/329,431 Expired - Lifetime US6274752B1 (en) | 1996-02-20 | 1999-06-10 | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
Country Status (1)
| Country | Link |
|---|---|
| US (2) | US6274752B1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060020517A1 (en) * | 2004-07-21 | 2006-01-26 | Smart Destinations Inc. | Programmable ticketing system |
| US20170046809A1 (en) * | 2015-04-06 | 2017-02-16 | Evelyn Laureano-Osorio | My Personal Identification Mobile Wallet |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1304181B1 (en) * | 1998-12-17 | 2001-03-08 | Enichem Spa | ACTIVATING COMPOSITION OF METALLOCENIC COMPLEXES IN THE CATALYSIS OF (CO) POLYMERIZATION OF OLEFINS. |
| US8012900B2 (en) * | 2007-12-28 | 2011-09-06 | Chevron Phillips Chemical Company, L.P. | Nano-linked metallocene catalyst compositions and their polymer products |
| US7863210B2 (en) | 2007-12-28 | 2011-01-04 | Chevron Phillips Chemical Company Lp | Nano-linked metallocene catalyst compositions and their polymer products |
| US8080681B2 (en) * | 2007-12-28 | 2011-12-20 | Chevron Phillips Chemical Company Lp | Nano-linked metallocene catalyst compositions and their polymer products |
| US7919639B2 (en) | 2009-06-23 | 2011-04-05 | Chevron Phillips Chemical Company Lp | Nano-linked heteronuclear metallocene catalyst compositions and their polymer products |
Family Cites Families (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3966453A (en) | 1972-01-27 | 1976-06-29 | Ishihara Sangyo Kaisha Ltd. | Herbicidal 2-halo-4-trifluoromethyl-4'-cyanophenyl-ethers |
| US3950435A (en) | 1972-01-27 | 1976-04-13 | Ishihara Sangyo Kaisha Ltd. | Herbicidal diphenyl ethers |
| IL85097A (en) | 1987-01-30 | 1992-02-16 | Exxon Chemical Patents Inc | Catalysts based on derivatives of a bis(cyclopentadienyl)group ivb metal compound,their preparation and their use in polymerization processes |
| US5384299A (en) | 1987-01-30 | 1995-01-24 | Exxon Chemical Patents Inc. | Ionic metallocene catalyst compositions |
| NZ235032A (en) | 1989-08-31 | 1993-04-28 | Dow Chemical Co | Constrained geometry complexes of titanium, zirconium or hafnium comprising a substituted cyclopentadiene ligand; use as olefin polymerisation catalyst component |
| US5064802A (en) | 1989-09-14 | 1991-11-12 | The Dow Chemical Company | Metal complex compounds |
| US5763549A (en) | 1989-10-10 | 1998-06-09 | Fina Technology, Inc. | Cationic metallocene catalysts based on organoaluminum anions |
| ES2087145T3 (en) | 1989-10-10 | 1996-07-16 | Fina Technology | METALLOCAN CATALYSTS WITH LEWIS ACIDS AND ALKYL-ALUMINUMS. |
| JP2545006B2 (en) | 1990-07-03 | 1996-10-16 | ザ ダウ ケミカル カンパニー | Addition polymerization catalyst |
| JPH04366109A (en) | 1991-06-12 | 1992-12-18 | Idemitsu Kosan Co Ltd | Method for producing styrenic polymer and its catalyst |
| US5391789A (en) | 1991-08-08 | 1995-02-21 | Hoechst Aktiengesellschaft | Bridged, chiral metallocenes, processes for their preparation and their use as catalysts |
| JP3371118B2 (en) | 1991-11-30 | 2003-01-27 | バーゼル・ポリオレフィン・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング | Metallocenes having benzene-fused indenyl derivatives as ligands, their preparation and their use as catalysts |
| FR2688783A1 (en) | 1992-03-23 | 1993-09-24 | Rhone Poulenc Chimie | NOVEL BORONES OF ONIUM OR ORGANOMETALLIC COMPLEX CATIONIC PRIMERS FOR POLYMERIZATION. |
| US5330948A (en) | 1992-03-31 | 1994-07-19 | Northwestern University | Homogeneous catalysts for stereoregular olefin polymerization |
| US5296433A (en) | 1992-04-14 | 1994-03-22 | Minnesota Mining And Manufacturing Company | Tris(pentafluorophenyl)borane complexes and catalysts derived therefrom |
| US5300598A (en) | 1992-10-16 | 1994-04-05 | Northwestern University | Method of polymerizing exo-methylene cyclic organic compounds using homogeneous ring-opening catalysts |
| US5332706A (en) | 1992-12-28 | 1994-07-26 | Mobil Oil Corporation | Process and a catalyst for preventing reactor fouling |
| US5602067A (en) | 1992-12-28 | 1997-02-11 | Mobil Oil Corporation | Process and a catalyst for preventing reactor fouling |
| DE69418088T2 (en) | 1993-04-06 | 1999-08-12 | Bp Chemicals Ltd., London | Catalyst composition |
| US5582764A (en) | 1994-03-01 | 1996-12-10 | Shin-Etsu Chemical Co., Ltd. | Silacyclohexane compound, a method of preparing it and a liquid crystal composition containing it |
| US5502017A (en) | 1994-03-10 | 1996-03-26 | Northwestern University | Metallocene catalyst containing bulky organic group |
| JP3369294B2 (en) | 1994-03-11 | 2003-01-20 | 出光興産株式会社 | Transition metal compound, polymerization catalyst using the same, and method for producing styrenic polymer using the polymerization catalyst |
| US5498581A (en) | 1994-06-01 | 1996-03-12 | Phillips Petroleum Company | Method for making and using a supported metallocene catalyst system |
| US5486632A (en) | 1994-06-28 | 1996-01-23 | The Dow Chemical Company | Group 4 metal diene complexes and addition polymerization catalysts therefrom |
| US5500398A (en) | 1994-11-09 | 1996-03-19 | Northwestern University | Homogeneous α-olefin dimerization catalysts |
| GB9423606D0 (en) | 1994-11-23 | 1995-01-11 | Piers Warren E | Method of producing base free ziegler-natta olefin polymerizaton catalysts using a new, highly electrophilic borane reagent |
| US5554775A (en) | 1995-01-17 | 1996-09-10 | Occidental Chemical Corporation | Borabenzene based olefin polymerization catalysts |
| IT1275856B1 (en) | 1995-03-03 | 1997-10-24 | Spherilene Srl | BIS-FLUORENYL METALLOCENE COMPOUNDS, PROCEDURE FOR THEIR PREPARATION AND THEIR USE IN CATALYSTS FOR POLYMERIZATION |
| US5721183A (en) | 1995-03-10 | 1998-02-24 | The Dow Chemical Company | Catalyst system comprising amine or phosphine adducts of tris(organyl)borane compounds |
| IT1275777B1 (en) | 1995-07-06 | 1997-10-17 | Enichem Spa | METALLOCENIC CATALYST FOR THE (CO) POLYMERIZATION OF OLEFINS |
| IT1277677B1 (en) | 1995-12-21 | 1997-11-11 | Enichem Spa | PROCEDURE FOR THE PREPARATION OF CRYSTALLINE VINYLAROMATIC POLYMERS WITH PREDOMINANTLY SYNDIOTACTIC STRUCTURE |
| US5856256A (en) | 1996-02-20 | 1999-01-05 | Northwestern University | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations |
| ES2147985T3 (en) | 1996-03-27 | 2000-10-01 | Dow Chemical Co | HIGHLY SOLUBLE OLEPHINE POLYMERIZATION CATALYST ACTIVATOR. |
| FI972230A7 (en) | 1997-01-28 | 1998-07-29 | Borealis As | New homogeneous olefin polymerization catalyst composition |
| US5756611A (en) | 1997-02-21 | 1998-05-26 | Lyondell Petrochemical Company | α-olefin polymerization catalysts |
| WO1998041530A1 (en) | 1997-03-17 | 1998-09-24 | Exxon Chemical Patents Inc. | Transition metal metallacyclopentadienyl compounds |
| CA2204803C (en) | 1997-05-08 | 2005-11-15 | Nova Chemicals Ltd. | Process to prepare bridged phosphole-cyclopentadienyl compounds |
| JPH1129576A (en) * | 1997-07-04 | 1999-02-02 | Nippon Shokubai Co Ltd | Stabilizer of (fluorinated aryl)boron compound, stabilization and crystallization |
-
1999
- 1999-06-10 US US09/329,431 patent/US6274752B1/en not_active Expired - Lifetime
-
2001
- 2001-07-05 US US09/899,698 patent/US6403733B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060020517A1 (en) * | 2004-07-21 | 2006-01-26 | Smart Destinations Inc. | Programmable ticketing system |
| US20170046809A1 (en) * | 2015-04-06 | 2017-02-16 | Evelyn Laureano-Osorio | My Personal Identification Mobile Wallet |
Also Published As
| Publication number | Publication date |
|---|---|
| US6403733B2 (en) | 2002-06-11 |
| US6274752B1 (en) | 2001-08-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6087460A (en) | Organo-Lewis acid as cocatalyst for cationic homogenous metallocene Ziegler-Natta olefin polymerizations | |
| AU665320B1 (en) | Unbridged indenyl-containing metallocenes useful in olefin polymerization | |
| US6291695B1 (en) | Organo-Lewis acids of enhanced utility, uses thereof, and products based thereon | |
| US5414180A (en) | Organo-aluminoxy product and use | |
| JP3014455B2 (en) | Monocyclopentadienyl metal compound for catalyst for producing ethylene-α-olefin copolymer | |
| EP0608054A2 (en) | Catalyst compositions and process for preparing polyolefins | |
| EP0958051A4 (en) | USE OF GROUP 13 METALLIC FLUORO PERFLUOROARYL ANIONS IN METALLOCENE CATALYSTS FOR OLEFIN POLYMERIZATION | |
| EP0528041A1 (en) | Novel transition metal compound and process for polymerizing olefin by using the same | |
| WO1998050392A1 (en) | Process to prepare bridged phosphole-cyclopentadienyl compounds | |
| KR19980702204A (en) | Olefin Polymerization Catalyst Based on Borabenzene | |
| WO2001081436A1 (en) | Olefin polymerizations using ionic liquids as solvents | |
| US5856258A (en) | Phenolate constrained geometry polymerization catalyst and method for preparing | |
| US5162466A (en) | Use of methylene-bridged derivatives of cyclopentadienyl dicarbollide complexes of titanium, zirconium and hafnium as polymerization catalysts | |
| US20040198930A1 (en) | Method for production of multimodal polyolefins of tunable composition, molecular weight, and polydispersity | |
| US6403733B2 (en) | Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations | |
| US5214173A (en) | Cyclopentadienyl dicarbollide complexes of titanium, zirconium and hafnium | |
| EP1066302B1 (en) | Cyclopentadienyl transition metal compounds, as polymerization catalysts | |
| US6130302A (en) | Synthesis and use of (polyfluoroaryl)fluoroanions of aluminum, gallium and indium | |
| US6262200B1 (en) | (Polyfluoroaryl)fluoroanions of aluminum, gallium, and indium of enhanced utility, uses thereof, and products based thereon | |
| EP1019421A1 (en) | Transition metal compound, a process for its preparation and its use as a catalyst component | |
| Marks et al. | Organo-Lewis acids of enhanced utility, uses thereof, and products based thereon | |
| JP3427488B2 (en) | Novel organic transition metal compound and method for producing polyolefin using the same | |
| CA2219816C (en) | Azaborolinyl metal complexes as olefin polymerization catalysts | |
| Jordan et al. | Cyclopentadienyl dicarbollide complexes of titanium, zirconium and hafnium | |
| WO1997042235A1 (en) | Process for the production of polymers containing cyclic olefins |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
|
| CC | Certificate of correction | ||
| AS | Assignment |
Owner name: UNITED STATES DEPARTMENT OF ENERGY, DISTRICT OF CO Free format text: CONFIRMATORY LICENSE;ASSIGNOR:NORTHWESTERN UNIVERSITY;REEL/FRAME:013541/0969 Effective date: 20021025 |
|
| FEPP | Fee payment procedure |
Free format text: PAT HOLDER CLAIMS SMALL ENTITY STATUS, ENTITY STATUS SET TO SMALL (ORIGINAL EVENT CODE: LTOS); ENTITY STATUS OF PATENT OWNER: MICROENTITY |
|
| FPAY | Fee payment |
Year of fee payment: 4 |
|
| REMI | Maintenance fee reminder mailed | ||
| FPAY | Fee payment |
Year of fee payment: 8 |
|
| SULP | Surcharge for late payment |
Year of fee payment: 7 |
|
| FEPP | Fee payment procedure |
Free format text: PATENT HOLDER CLAIMS MICRO ENTITY STATUS, ENTITY STATUS SET TO MICRO (ORIGINAL EVENT CODE: STOM); ENTITY STATUS OF PATENT OWNER: MICROENTITY |
|
| FPAY | Fee payment |
Year of fee payment: 12 |