WO2004056478A1 - Tetramerization of olefins - Google Patents
Tetramerization of olefins Download PDFInfo
- Publication number
- WO2004056478A1 WO2004056478A1 PCT/ZA2003/000186 ZA0300186W WO2004056478A1 WO 2004056478 A1 WO2004056478 A1 WO 2004056478A1 ZA 0300186 W ZA0300186 W ZA 0300186W WO 2004056478 A1 WO2004056478 A1 WO 2004056478A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- methoxyphenyl
- phenyl
- catalyst system
- transition metal
- group
- Prior art date
Links
- 150000001336 alkenes Chemical class 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 claims abstract description 108
- 239000003054 catalyst Substances 0.000 claims abstract description 91
- 239000003446 ligand Substances 0.000 claims abstract description 72
- 150000003623 transition metal compounds Chemical class 0.000 claims abstract description 27
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims abstract description 17
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 106
- 239000005977 Ethylene Substances 0.000 claims description 106
- 125000004172 4-methoxyphenyl group Chemical group [H]C1=C([H])C(OC([H])([H])[H])=C([H])C([H])=C1* 0.000 claims description 88
- -1 methylene, dimethylmethylene Chemical group 0.000 claims description 81
- CPOFMOWDMVWCLF-UHFFFAOYSA-N methyl(oxo)alumane Chemical compound C[Al]=O CPOFMOWDMVWCLF-UHFFFAOYSA-N 0.000 claims description 56
- 239000000203 mixture Substances 0.000 claims description 46
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 claims description 44
- 125000001424 substituent group Chemical group 0.000 claims description 44
- 125000004429 atom Chemical group 0.000 claims description 43
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 43
- 238000002156 mixing Methods 0.000 claims description 35
- 239000011651 chromium Substances 0.000 claims description 32
- 229910052723 transition metal Inorganic materials 0.000 claims description 32
- 150000003624 transition metals Chemical class 0.000 claims description 32
- 125000003118 aryl group Chemical group 0.000 claims description 27
- 125000004207 3-methoxyphenyl group Chemical group [H]C1=C([H])C(*)=C([H])C(OC([H])([H])[H])=C1[H] 0.000 claims description 26
- 239000012190 activator Substances 0.000 claims description 24
- 150000001875 compounds Chemical class 0.000 claims description 24
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 23
- 125000001183 hydrocarbyl group Chemical group 0.000 claims description 23
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 21
- 239000011541 reaction mixture Substances 0.000 claims description 21
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 20
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 20
- BFGKITSFLPAWGI-UHFFFAOYSA-N chromium(3+) Chemical compound [Cr+3] BFGKITSFLPAWGI-UHFFFAOYSA-N 0.000 claims description 20
- 125000005647 linker group Chemical group 0.000 claims description 20
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 16
- 229910052804 chromium Inorganic materials 0.000 claims description 16
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 claims description 16
- 229910052757 nitrogen Inorganic materials 0.000 claims description 16
- 229910052698 phosphorus Inorganic materials 0.000 claims description 16
- 239000011574 phosphorus Substances 0.000 claims description 16
- 229910052751 metal Inorganic materials 0.000 claims description 15
- 239000002184 metal Substances 0.000 claims description 15
- 239000004711 α-olefin Substances 0.000 claims description 14
- YVSMQHYREUQGRX-UHFFFAOYSA-N 2-ethyloxaluminane Chemical compound CC[Al]1CCCCO1 YVSMQHYREUQGRX-UHFFFAOYSA-N 0.000 claims description 13
- 150000003839 salts Chemical class 0.000 claims description 12
- 150000004696 coordination complex Chemical class 0.000 claims description 11
- 229910052787 antimony Inorganic materials 0.000 claims description 9
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 claims description 9
- 229910052785 arsenic Inorganic materials 0.000 claims description 9
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims description 9
- 229910052797 bismuth Inorganic materials 0.000 claims description 9
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 9
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 229910052711 selenium Inorganic materials 0.000 claims description 9
- 239000011669 selenium Substances 0.000 claims description 9
- 125000004104 aryloxy group Chemical group 0.000 claims description 8
- 239000004305 biphenyl Substances 0.000 claims description 8
- 235000010290 biphenyl Nutrition 0.000 claims description 8
- WBKDDMYJLXVBNI-UHFFFAOYSA-K chromium(3+);2-ethylhexanoate Chemical compound [Cr+3].CCCCC(CC)C([O-])=O.CCCCC(CC)C([O-])=O.CCCCC(CC)C([O-])=O WBKDDMYJLXVBNI-UHFFFAOYSA-K 0.000 claims description 8
- 229910052736 halogen Inorganic materials 0.000 claims description 8
- 150000002367 halogens Chemical class 0.000 claims description 8
- 125000001072 heteroaryl group Chemical group 0.000 claims description 8
- 125000005842 heteroatom Chemical group 0.000 claims description 8
- 125000001624 naphthyl group Chemical group 0.000 claims description 8
- 230000003647 oxidation Effects 0.000 claims description 8
- 238000007254 oxidation reaction Methods 0.000 claims description 8
- 229910052717 sulfur Inorganic materials 0.000 claims description 8
- 125000003944 tolyl group Chemical group 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 238000011065 in-situ storage Methods 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 6
- GDOPTJXRTPNYNR-UHFFFAOYSA-N methylcyclopentane Chemical compound CC1CCCC1 GDOPTJXRTPNYNR-UHFFFAOYSA-N 0.000 claims description 6
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 claims description 6
- 125000002524 organometallic group Chemical group 0.000 claims description 6
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 claims description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 5
- 239000005864 Sulphur Substances 0.000 claims description 5
- 150000002899 organoaluminium compounds Chemical class 0.000 claims description 5
- DIIIISSCIXVANO-UHFFFAOYSA-N 1,2-Dimethylhydrazine Chemical compound CNNC DIIIISSCIXVANO-UHFFFAOYSA-N 0.000 claims description 4
- 125000002030 1,2-phenylene group Chemical group [H]C1=C([H])C([*:1])=C([*:2])C([H])=C1[H] 0.000 claims description 4
- 125000004198 2-fluorophenyl group Chemical group [H]C1=C([H])C(F)=C(*)C([H])=C1[H] 0.000 claims description 4
- 125000001255 4-fluorophenyl group Chemical group [H]C1=C([H])C(*)=C([H])C([H])=C1F 0.000 claims description 4
- UQRONKZLYKUEMO-UHFFFAOYSA-N 4-methyl-1-(2,4,6-trimethylphenyl)pent-4-en-2-one Chemical group CC(=C)CC(=O)Cc1c(C)cc(C)cc1C UQRONKZLYKUEMO-UHFFFAOYSA-N 0.000 claims description 4
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 4
- 125000003545 alkoxy group Chemical group 0.000 claims description 4
- 125000004453 alkoxycarbonyl group Chemical group 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000002178 anthracenyl group Chemical group C1(=CC=CC2=CC3=CC=CC=C3C=C12)* 0.000 claims description 4
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 claims description 4
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 4
- 125000003917 carbamoyl group Chemical group [H]N([H])C(*)=O 0.000 claims description 4
- 125000006297 carbonyl amino group Chemical group [H]N([*:2])C([*:1])=O 0.000 claims description 4
- 125000005708 carbonyloxy group Chemical group [*:2]OC([*:1])=O 0.000 claims description 4
- RPBPCPJJHKASGQ-UHFFFAOYSA-K chromium(3+);octanoate Chemical compound [Cr+3].CCCCCCCC([O-])=O.CCCCCCCC([O-])=O.CCCCCCCC([O-])=O RPBPCPJJHKASGQ-UHFFFAOYSA-K 0.000 claims description 4
- CYOMBOLDXZUMBU-UHFFFAOYSA-K chromium(3+);oxolane;trichloride Chemical compound [Cl-].[Cl-].[Cl-].[Cr+3].C1CCOC1.C1CCOC1.C1CCOC1 CYOMBOLDXZUMBU-UHFFFAOYSA-K 0.000 claims description 4
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 claims description 4
- 125000001511 cyclopentyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C1([H])[H] 0.000 claims description 4
- 125000004663 dialkyl amino group Chemical group 0.000 claims description 4
- NXPHGHWWQRMDIA-UHFFFAOYSA-M magnesium;carbanide;bromide Chemical compound [CH3-].[Mg+2].[Br-] NXPHGHWWQRMDIA-UHFFFAOYSA-M 0.000 claims description 4
- NFJPEKRRHIYYES-UHFFFAOYSA-N methylidenecyclopentane Chemical compound C=C1CCCC1 NFJPEKRRHIYYES-UHFFFAOYSA-N 0.000 claims description 4
- DVSDBMFJEQPWNO-UHFFFAOYSA-N methyllithium Chemical compound C[Li] DVSDBMFJEQPWNO-UHFFFAOYSA-N 0.000 claims description 4
- 150000007522 mineralic acids Chemical class 0.000 claims description 4
- 229910052750 molybdenum Inorganic materials 0.000 claims description 4
- 239000011733 molybdenum Substances 0.000 claims description 4
- 239000001294 propane Substances 0.000 claims description 4
- 125000004368 propenyl group Chemical group C(=CC)* 0.000 claims description 4
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 4
- 125000002568 propynyl group Chemical group [*]C#CC([H])([H])[H] 0.000 claims description 4
- 125000004076 pyridyl group Chemical group 0.000 claims description 4
- 229910001494 silver tetrafluoroborate Inorganic materials 0.000 claims description 4
- 125000003808 silyl group Chemical group [H][Si]([H])([H])[*] 0.000 claims description 4
- 125000000547 substituted alkyl group Chemical group 0.000 claims description 4
- 125000003107 substituted aryl group Chemical group 0.000 claims description 4
- 229910052715 tantalum Inorganic materials 0.000 claims description 4
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 claims description 4
- 125000003718 tetrahydrofuranyl group Chemical group 0.000 claims description 4
- 125000001544 thienyl group Chemical group 0.000 claims description 4
- 125000004014 thioethyl group Chemical group [H]SC([H])([H])C([H])([H])* 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 125000000026 trimethylsilyl group Chemical group [H]C([H])([H])[Si]([*])(C([H])([H])[H])C([H])([H])[H] 0.000 claims description 4
- LOFJKBAHPJENQS-UHFFFAOYSA-N tris(oxomethylidene)chromium Chemical compound O=C=[Cr](=C=O)=C=O LOFJKBAHPJENQS-UHFFFAOYSA-N 0.000 claims description 4
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 4
- 229910052721 tungsten Inorganic materials 0.000 claims description 4
- 239000010937 tungsten Substances 0.000 claims description 4
- 229910052720 vanadium Inorganic materials 0.000 claims description 4
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 claims description 4
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 4
- 125000005023 xylyl group Chemical group 0.000 claims description 4
- 229910052726 zirconium Inorganic materials 0.000 claims description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N dimethylmethane Natural products CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000000178 monomer Substances 0.000 claims description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims 4
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 claims 2
- 229910017053 inorganic salt Inorganic materials 0.000 claims 2
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 153
- 239000000047 product Substances 0.000 description 55
- 238000006243 chemical reaction Methods 0.000 description 40
- 239000000243 solution Substances 0.000 description 36
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 30
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 30
- 238000004458 analytical method Methods 0.000 description 30
- BKIMMITUMNQMOS-UHFFFAOYSA-N nonane Chemical compound CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 description 30
- 239000012044 organic layer Substances 0.000 description 30
- 238000000769 gas chromatography-flame ionisation detection Methods 0.000 description 21
- 238000009826 distribution Methods 0.000 description 18
- 239000004698 Polyethylene Substances 0.000 description 17
- 239000007788 liquid Substances 0.000 description 17
- 229920000573 polyethylene Polymers 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 239000007789 gas Substances 0.000 description 16
- 239000007791 liquid phase Substances 0.000 description 16
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 15
- 238000001816 cooling Methods 0.000 description 15
- 239000007787 solid Substances 0.000 description 15
- 239000012265 solid product Substances 0.000 description 15
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 12
- 239000000306 component Substances 0.000 description 11
- 239000007795 chemical reaction product Substances 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 7
- 239000002904 solvent Substances 0.000 description 7
- JLTRXTDYQLMHGR-UHFFFAOYSA-N trimethylaluminium Chemical compound C[Al](C)C JLTRXTDYQLMHGR-UHFFFAOYSA-N 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 4
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 4
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000012442 inert solvent Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N tetrahydrofuran Substances C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 239000013065 commercial product Substances 0.000 description 3
- 125000004122 cyclic group Chemical group 0.000 description 3
- UAOMVDZJSHZZME-UHFFFAOYSA-N diisopropylamine Chemical compound CC(C)NC(C)C UAOMVDZJSHZZME-UHFFFAOYSA-N 0.000 description 3
- REJGOFYVRVIODZ-UHFFFAOYSA-N phosphanium;chloride Chemical class P.Cl REJGOFYVRVIODZ-UHFFFAOYSA-N 0.000 description 3
- MCULRUJILOGHCJ-UHFFFAOYSA-N triisobutylaluminium Chemical compound CC(C)C[Al](CC(C)C)CC(C)C MCULRUJILOGHCJ-UHFFFAOYSA-N 0.000 description 3
- OBETXYAYXDNJHR-UHFFFAOYSA-N 2-Ethylhexanoic acid Chemical compound CCCCC(CC)C(O)=O OBETXYAYXDNJHR-UHFFFAOYSA-N 0.000 description 2
- UYRPRYSDOVYCOU-UHFFFAOYSA-N 2-diphenylphosphanylbenzoic acid Chemical compound OC(=O)C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 UYRPRYSDOVYCOU-UHFFFAOYSA-N 0.000 description 2
- 239000007818 Grignard reagent Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000006664 bond formation reaction Methods 0.000 description 2
- UORVGPXVDQYIDP-UHFFFAOYSA-N borane Chemical compound B UORVGPXVDQYIDP-UHFFFAOYSA-N 0.000 description 2
- SHZIWNPUGXLXDT-UHFFFAOYSA-N caproic acid ethyl ester Natural products CCCCCC(=O)OCC SHZIWNPUGXLXDT-UHFFFAOYSA-N 0.000 description 2
- YTFQUBRFOJIJOZ-UHFFFAOYSA-N chloro-bis(4-methoxyphenyl)phosphane Chemical compound C1=CC(OC)=CC=C1P(Cl)C1=CC=C(OC)C=C1 YTFQUBRFOJIJOZ-UHFFFAOYSA-N 0.000 description 2
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 2
- 150000004795 grignard reagents Chemical class 0.000 description 2
- 150000002431 hydrogen Chemical group 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 2
- UAEPNZWRGJTJPN-UHFFFAOYSA-N methylcyclohexane Chemical compound CC1CCCCC1 UAEPNZWRGJTJPN-UHFFFAOYSA-N 0.000 description 2
- 125000004092 methylthiomethyl group Chemical group [H]C([H])([H])SC([H])([H])* 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 125000004433 nitrogen atom Chemical group N* 0.000 description 2
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- KDIAMAVWIJYWHN-UHFFFAOYSA-N propylcyclopentane Chemical compound CCCC1CCCC1 KDIAMAVWIJYWHN-UHFFFAOYSA-N 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229910021653 sulphate ion Inorganic materials 0.000 description 2
- 125000002088 tosyl group Chemical group [H]C1=C([H])C(=C([H])C([H])=C1C([H])([H])[H])S(*)(=O)=O 0.000 description 2
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 2
- CRSBERNSMYQZNG-UHFFFAOYSA-N 1 -dodecene Natural products CCCCCCCCCCC=C CRSBERNSMYQZNG-UHFFFAOYSA-N 0.000 description 1
- AZUYLZMQTIKGSC-UHFFFAOYSA-N 1-[6-[4-(5-chloro-6-methyl-1H-indazol-4-yl)-5-methyl-3-(1-methylindazol-5-yl)pyrazol-1-yl]-2-azaspiro[3.3]heptan-2-yl]prop-2-en-1-one Chemical compound ClC=1C(=C2C=NNC2=CC=1C)C=1C(=NN(C=1C)C1CC2(CN(C2)C(C=C)=O)C1)C=1C=C2C=NN(C2=CC=1)C AZUYLZMQTIKGSC-UHFFFAOYSA-N 0.000 description 1
- QNJUXDQESJRITJ-UHFFFAOYSA-N 2-diethylphosphanyl-n-(2-diethylphosphanylethyl)ethanamine Chemical compound CCP(CC)CCNCCP(CC)CC QNJUXDQESJRITJ-UHFFFAOYSA-N 0.000 description 1
- QJPJQTDYNZXKQF-UHFFFAOYSA-N 4-bromoanisole Chemical compound COC1=CC=C(Br)C=C1 QJPJQTDYNZXKQF-UHFFFAOYSA-N 0.000 description 1
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- 125000006539 C12 alkyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- KBSCQVGRWYLGED-UHFFFAOYSA-N N-diaminophosphoryl-N-propan-2-ylpropan-2-amine dihydrochloride Chemical compound Cl.Cl.CC(C)N(C(C)C)P(N)(N)=O KBSCQVGRWYLGED-UHFFFAOYSA-N 0.000 description 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000007983 Tris buffer Substances 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 125000005234 alkyl aluminium group Chemical group 0.000 description 1
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229910000085 borane Inorganic materials 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000007806 chemical reaction intermediate Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- SYMNFHBCGCJJEY-UHFFFAOYSA-N cyclopentane prop-1-ene Chemical compound C1CCCC1.C=CC SYMNFHBCGCJJEY-UHFFFAOYSA-N 0.000 description 1
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 0.000 description 1
- 229940043279 diisopropylamine Drugs 0.000 description 1
- JGHYBJVUQGTEEB-UHFFFAOYSA-M dimethylalumanylium;chloride Chemical compound C[Al](C)Cl JGHYBJVUQGTEEB-UHFFFAOYSA-M 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 229940069096 dodecene Drugs 0.000 description 1
- UAIZDWNSWGTKFZ-UHFFFAOYSA-L ethylaluminum(2+);dichloride Chemical compound CC[Al](Cl)Cl UAIZDWNSWGTKFZ-UHFFFAOYSA-L 0.000 description 1
- 238000011066 ex-situ storage Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002608 ionic liquid Substances 0.000 description 1
- JJWLVOIRVHMVIS-UHFFFAOYSA-N isopropylamine Chemical compound CC(C)N JJWLVOIRVHMVIS-UHFFFAOYSA-N 0.000 description 1
- RBWRWAUAVRMBAC-UHFFFAOYSA-M magnesium;methoxybenzene;bromide Chemical compound [Mg+2].[Br-].COC1=CC=[C-]C=C1 RBWRWAUAVRMBAC-UHFFFAOYSA-M 0.000 description 1
- GYNNXHKOJHMOHS-UHFFFAOYSA-N methyl-cycloheptane Natural products CC1CCCCCC1 GYNNXHKOJHMOHS-UHFFFAOYSA-N 0.000 description 1
- YSTQWZZQKCCBAY-UHFFFAOYSA-L methylaluminum(2+);dichloride Chemical compound C[Al](Cl)Cl YSTQWZZQKCCBAY-UHFFFAOYSA-L 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- AFFLGGQVNFXPEV-UHFFFAOYSA-N n-decene Natural products CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 1
- 150000002816 nickel compounds Chemical class 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- WWZKQHOCKIZLMA-UHFFFAOYSA-M octanoate Chemical compound CCCCCCCC([O-])=O WWZKQHOCKIZLMA-UHFFFAOYSA-M 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 125000004437 phosphorous atom Chemical group 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000000066 reactive distillation Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- LGQXXHMEBUOXRP-UHFFFAOYSA-N tributyl borate Chemical compound CCCCOB(OCCCC)OCCCC LGQXXHMEBUOXRP-UHFFFAOYSA-N 0.000 description 1
- LALRXNPLTWZJIJ-UHFFFAOYSA-N triethylborane Chemical compound CCB(CC)CC LALRXNPLTWZJIJ-UHFFFAOYSA-N 0.000 description 1
- LFXVBWRMVZPLFK-UHFFFAOYSA-N trioctylalumane Chemical compound CCCCCCCC[Al](CCCCCCCC)CCCCCCCC LFXVBWRMVZPLFK-UHFFFAOYSA-N 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/26—Catalytic processes with hydrides or organic compounds
- C07C2/36—Catalytic processes with hydrides or organic compounds as phosphines, arsines, stilbines or bismuthines
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/26—Catalytic processes with hydrides or organic compounds
- C07C2/32—Catalytic processes with hydrides or organic compounds as complexes, e.g. acetyl-acetonates
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/12—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides
- B01J31/14—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
- B01J31/143—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron of aluminium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
-
- 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
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1805—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing nitrogen
-
- 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
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1845—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
- B01J31/1865—Phosphonites (RP(OR)2), their isomeric phosphinates (R2(RO)P=O) and RO-substitution derivatives thereof
- B01J31/187—Amide derivatives thereof
-
- 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
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1845—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
- B01J31/1875—Phosphinites (R2P(OR), their isomeric phosphine oxides (R3P=O) and RO-substitution derivatives thereof)
- B01J31/188—Amide derivatives thereof
-
- 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
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1845—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
- B01J31/1885—Ligands comprising two different formal oxidation states of phosphorus in one at least bidentate ligand, e.g. phosphite/phosphinite
-
- 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
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
-
- 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
- B01J31/24—Phosphines, i.e. phosphorus bonded to only carbon atoms, or to both carbon and hydrogen atoms, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, phosphole or anionic phospholide ligands
- B01J31/2404—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring
- B01J31/2409—Cyclic ligands, including e.g. non-condensed polycyclic ligands, the phosphine-P atom being a ring member or a substituent on the ring with more than one complexing phosphine-P atom
-
- 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
- C07F11/00—Compounds containing elements of Groups 6 or 16 of the Periodic Table
- C07F11/005—Compounds containing elements of Groups 6 or 16 of the Periodic Table compounds without a metal-carbon linkage
-
- 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
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/20—Olefin oligomerisation or telomerisation
-
- 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
- B01J2531/50—Complexes comprising metals of Group V (VA or VB) as the central metal
- B01J2531/56—Vanadium
-
- 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
- B01J2531/50—Complexes comprising metals of Group V (VA or VB) as the central metal
- B01J2531/58—Tantalum
-
- 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
- B01J2531/60—Complexes comprising metals of Group VI (VIA or VIB) as the central metal
- B01J2531/62—Chromium
-
- 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
- B01J2531/60—Complexes comprising metals of Group VI (VIA or VIB) as the central metal
- B01J2531/64—Molybdenum
-
- 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
- B01J2531/60—Complexes comprising metals of Group VI (VIA or VIB) as the central metal
- B01J2531/66—Tungsten
-
- 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
- B01J31/128—Mixtures of organometallic compounds
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/1616—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/165—Polymer immobilised coordination complexes, e.g. organometallic complexes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- C07C2531/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- C07C2531/12—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides
- C07C2531/14—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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- C07C2531/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- C07C2531/24—Phosphines
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- C07C2531/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups C07C2531/02 - C07C2531/24
- C07C2531/34—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups C07C2531/02 - C07C2531/24 of chromium, molybdenum or tungsten
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2410/00—Features related to the catalyst preparation, the catalyst use or to the deactivation of the catalyst
- C08F2410/03—Multinuclear procatalyst, i.e. containing two or more metals, being different or not
-
- 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
- C08F4/639—Component covered by group C08F4/62 containing a transition metal-carbon bond
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/6592—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/6592—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
- C08F4/65922—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not
- C08F4/65927—Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not two cyclopentadienyl rings being mutually bridged
Definitions
- This invention relates to the oligomerisation of ethylene. More particularly, the invention relates to a tetramerisation process, a catalyst system for tetramerisation of olefins and the identification and use of ligands for a catalyst system for tetramerisation of olefins.
- This invention defines a process and catalyst system, that facilitates the production of 1- octene in high selectivity, while avoiding the co-production of significant quantities of butenes, other octene isomers, specific higher oligomers and polyethylene.
- the catalyst system can also be used for the tetramerisation of other olefins, especially ⁇ -olefins.
- a nickel catalyst comprising a chelating ligand, preferably 2-diphenyl phosphino benzoic acid (DPPBA), a nickel compound, preferably NiCI 2 .6H 2 O, and a catalyst activator, preferably sodium tetraphenylborate, catalyse the oligomerisation of ethylene to yield a mixture of linear olefins.
- DPPBA 2-diphenyl phosphino benzoic acid
- a nickel compound preferably NiCI 2 .6H 2 O
- a catalyst activator preferably sodium tetraphenylborate
- Ziegler-type technologies based on trialkylaluminium catalysts are also commercially used to oligomerise ethylene to mixtures of olefins that reportedly contain 13-25 mass % 1- octene (Chem Systems PERP reports 90-1 , 93-6, and 94/95S12).
- chromium-based catalysts containing heteroatomic ligands with both phosphorus and nitrogen heteroatoms selectively catalyse the trimerisation of ethylene to 1-hexene.
- heteroatomic ligands for ethylene trimerisation include bis(2-diethylphosphino-ethyl) amine (WO 03/053891 , hereby fully incorporated herein by means of reference) as well as (o- methoxyphenyl) 2 PN(methyl)P(o-methoxyphenyl) 2 (WO 02/04119, hereby fully incorporated herein by means of reference).
- chromium-based catalysts containing mixed heteroatomic ligands with both nitrogen and phosphorus heteroatoms, with polar substituents on the hydrocarbyl or heterohydrocarbyl groups on the phosphorous atoms can be used to selectively tetramerise ethylene to 1 -octene often in excess of 60 mass% selectivity.
- This high 1- octene selectivity cannot be achieved via conventional one-step ethylene oligomerisation or trimerisation technologies which at most yield 25 mass% 1 -octene.
- This invention relates to a process for selectively producing tetrameric products.
- This invention specifically relates to a process for selectively producing tetrameric products such as 1 -octene from olefins such as ethylene.
- the invention relates to a process of selectively producing tetrametric products using a transition metal catalyst system containing a heteroatomic ligand.
- a process for tetramerisation of olefins wherein the product of the tetramerisation process is an olefin and makes up more than 30% of the product stream of the process.
- the tetramerisation process includes the step of contacting an olefinic feedstream with a catalyst system which includes a transition metal and a heteroatomic ligand and wherein the product of the tetramerisation process is an olefin and makes up more than 30% of the product stream of the process.
- % will be understood to be a mass %.
- tetramerisation generally refers to the reaction of four, and preferably four identical, olefinic monomer units to yield a linear and/or branched olefin.
- heteroatomic a ligand that contains at least two heteroatoms, which can be the same or different, where the heteroatoms may be selected from phosphorus, arsenic, antimony, sulphur, oxygen, bismuth, selenium or nitrogen.
- the feedstream will be understood to include an olefin to be tetramerised and can be introduced into the process according to the invention in a continuous or batch fashion.
- the product stream will be understood to include a tetramer, which tetramer is produced according to the invention in a continuous or batch fashion.
- the feedstream may include an ⁇ -olefin and the product stream may include at least 30%, preferably at least 35%, of a tetramerised ⁇ -olefin monomer.
- the process may include a process for tetramerisation of ⁇ -olefins.
- ⁇ - olefins is meant all hydrocarbon compounds with terminal double bonds. This definition includes ethylene, propylene, 1-butene, isobutylene, 1-pentene, 1-hexene, 1 -octene and the like.
- the process may include a process for tetramerisation of ⁇ -olefins to selectively yield tetrameric ⁇ -olefin products.
- the olefinic feedstream may include ethylene and the product stream may include at least 30% 1 -octene.
- the process may be a process for tetramerisation of ethylene.
- the invention allows the ligand, catalyst system and/or process conditions to be selected to give a product stream of more than 40%, 50%, or 60% ⁇ -olefins. It may be preferable, depending on the further use of the product stream, to have such high selectivities of the ⁇ -olefin.
- the olefinic feedstream may include ethylene and the (C 6 + C 8 ) : (C 4 + C 10 ) ratio in the product stream may be more than 2.5:1.
- the olefinic feedstream may include ethylene and the C 8 : C 6 ratio in the product stream is more than 1.
- the ethylene may be contacted with the catalyst system at a pressure of greater than 1 barg and preferably greater than 10 barg, more preferably greater than 30 barg.
- the heteroatomic ligand may be described by the following general formula (R) n A-B-C(R) m where A and C are independently selected from a group which comprises phosphorus, arsenic, antimony, oxygen, bismuth, sulphur, selenium, and nitrogen, and B is a linking group between A and C, and R is independently selected from any homo or heterohydrocarbyl group of which at least one R group is substituted with a polar substituent and n and m is determined by the respective valence and oxidation state of A and C.
- a and/or C may be a potential electron donor for coordination with the transition metal.
- An electron donor or electron donating substituent is defined as that entity that donates electrons used in chemical, including dative covalent, bond formation.
- the heteroatomic ligand may be described by the following general formula (R 1 )(R 2 )A-B- C(R 3 )(R 4 ) where A and C are independently selected from a group which comprises phosphorus, arsenic, antimony, bismuth and nitrogen and B is a linking group between A and C, and R 1 , R 2 , R 3 and R 4 are independently selected from non-aromatic and aromatic, including heteroaromatic, groups of which at least one of R 1 , R 2 , R 3 and R 4 is substituted with a polar substituent.
- R 1 , R 2 , R 3 and R 4 may have substituents on the atom adjacent to the atom bound to A or C.
- each of R 1 , R 2 , R 3 and R 4 may be aromatic, including heteroaromatic, but preferably not all of R 1 , R 2 , R 3 and R 4 , if they all are aromatic, are substituted by any substituent on an atom adjacent to the atom bound to A or C.
- R 1 , R 2 , R 3 and R 4 may have substituents on the atom adjacent to the atom bound to A or C.
- Any polar substituents on R 1 , R 2 , R 3 and R 4 may preferably not be on the atom adjacent to the atom bound to A or C.
- At least one of R 1 , R 2 , R 3 and R 4 may be substituted with a polar substituent on the 2 nd or further atom from the atom bound to A or C.
- Any polar substituent on one or more of R 1 , R 2 , R 3 and R 4 may be electron donating.
- Polar is defined by IUPAC as an entity with a permanent electric dipole moment.
- Polar substituents include methoxy, ethoxy, isopropoxy, C 3 -C 20 alkoxy, phenoxy, pentafluorophenoxy, trimethylsiloxy, dimethylamino, methylsulfanyl, tosyl, methoxymethy, methylthiomethyl, 1 ,3-oxazolyl, methomethoxy, hydroxyl, amino, phosphino, arsino, stibino, sulphate, nitro and the like.
- any of the groups R 1 , R 2 , R 3 and R 4 may independently be linked to one or more of each other or to the linking group B to form a cyclic structure together with A and C, A and B or B and C.
- R 1 , R 2 , R 3 and R 4 may be independently selected from a group comprising a benzyl, phenyl, tolyl, xylyl, mesityl, biphenyl, naphthyl, anthracenyl, methoxy, ethoxy, phenoxy, tolyloxy, dimethylamino, diethylamino, methylethylamino, thiophenyl, pyridyl, thioethyl, thiophenoxy, trimethylsilyl, dimethylhydrazyl, methyl, ethyl, ethenyl, propyl, butyl, propenyl, propynyl, cyclopentyl, cyclohexyl, ferrocenyl and tetrahydrofuranyl group.
- R 1 , R 2 , R 3 and R 4 may independently be selected from a group comprising a phenyl, tolyl,
- a and/or C may be independently oxidised by S, Se, N or O, where the valence of A and/or C allows for such oxidation.
- a and C may be independently phosphorus or phosphorus oxidised by S or Se or N or O.
- B may be selected from any one of a group comprising: organic linking groups comprising a hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl and a substituted heterohydrocarbyl; inorganic linking groups comprising single atom links; ionic links; and a group comprising methylene, dimethylmethylene, 1 ,2-ethane, 1 ,2-phenylene, 1 ,2- propane, 1 ,2-catechol, 1 ,2-dimethylhydrazine, -B(R 5 )-, -Si(R 5 ) 2 -, -P(R 5 )- and -N(R 5 )- where R 5 is hydrogen, a hydrocarbyl or substituted hydrocarbyl, a substituted heteroatom or a halogen.
- B may be -N(R 5 )- and R 5 is a hydrocarbyl or a substituted hydrocarbyl group.
- R 5 may be hydrogen or may be selected from the groups consisting of alkyl, substituted alkyl, aryl, substituted aryl, aryloxy, substituted aryloxy, halogen, nitro, alkoxycarbonyl, carbonyloxy, alkoxy, aminocarbonyl, carbonylamino, dialkylamino, silyl groups or derivatives thereof, and aryl substituted with any of these substituents.
- R 5 may be an isopropyl, a 1-cyclohexylethyl, a 2- methylcyclohexyl or a 2-octyl group.
- a single atom linking spacer is defined as a substituted or non-substituted atom that is bound directly to A and C.
- the ligand may also contain multiple (R) n A-B-C(R) m units.
- Non limiting examples of such ligands include dendrimeric ligands as well as ligands where the individual units are coupled either via one or more of the R groups or via the linking group B . More specific, but non limiting, examples of such ligands may include 1 ,2-di-(N(P(4- methoxyphenyl) 2 ) 2 )-benzene, 1 ,4-di-(N(P(4-methoxyphenyl) 2 ) 2 )-benzene,
- ligands are: (3- methoxyphenyl) 2 PN(methyl)P(3-methoxyphenyl) 2, (4-methoxyphenyl) 2 PN(methyl)P(4- methoxyphenyl) 2 , (3-methoxyphenyl) 2 PN(isopropyl)P(3-methoxyphenyl) 2 ,(4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 , (4-methoxyphenyl) 2 PN(2- ethylhexyl)P(4-methoxyphenyl) 2 , (3-methoxyphenyl)(phenyl)PN(methyl)P(phenyl) 2 and (4-methoxyphenyl)(phenyl)PN(methyl)P(phenyl) 2 , (3- methoxyphenyl)(phenyl)PN(methyl)P(3-methoxyphenyl)(phenyl)
- the catalyst system may include an activator and the process may include the step of combining in any order a heteroatomic ligand with a transition metal compound and an activator.
- the process may include the step of generating a heteroatomic coordination complex in situ from a transition metal compound and a heteroatomic ligand.
- the process may include the step of adding a pre-formed coordination complex, prepared using a heteroatomic ligand and a transition metal compound, to a reaction mixture, or the step of adding separately to the reactor, a heteroatomic ligand and a transition metal compound such that a heteroatomic coordination complex of a transition metal is generated in situ.
- generating a heteroatomic coordination complex in situ is meant that the complex is generated in the medium in which catalysis takes place.
- the heteroatomic coordination complex is generated in situ.
- the transition metal compound, and heteroatomic ligand are combined (both in situ and ex situ) to provide metal/ligand ratios from about 0.01:100 to 10 000:1, and preferably, from about 0.1 :1 to 10:1.
- the transition metal may be selected from any one of a group comprising chromium, molybdenum, tungsten, titanium, tantalum, vanadium and zirconium, preferably chromium.
- the transition metal compound which, upon mixing with the heteroatomic ligand and an activator, catalyses ethylene tetramerisation in accordance with the invention may be a simple inorganic or organic salt, a co-ordination or organometallic complex and may be selected from any one of a group comprising chromium trichloride tris-tetrahydrofuran complex, (benzene)tricarbonyl chromium, chromium (III) octanoate, chromium hexacarbonyl, chromium (III) acetylacetonoate and chromium (III) 2-ethylhexanoate.
- the preferred transition metal compounds include chromium (III) acetylacetonoate and chromium (III) 2-ethylhexanoate.
- the heteroatomic ligand can be modified to be attached to a polymer chain so that the resulting heteroatomic coordination complex of the transition metal is soluble at elevated temperatures, but becomes insoluble at 25°C.
- This approach would enable the recovery of the complex from the reaction mixture for reuse and has been used for other catalyst as described by D.E. Bergbreiter et al., J. Am. Chem. Soc, 1987, 109, 177-179.
- these transition metal complexes can also be immobilised by binding the heteroatomic ligands for example to silica, silica gel, polysiloxane, alumina backbone or the like as demonstrated, for example, by C. Yuanyin et al., Chinese J. React. Pol., 1992, 1(2), 152-159 for immobilising platinum complexes.
- the activator for use in the process may in principle be any compound that generates an active catalyst when combined with the heteroatomic ligand and the transition metal compound. Mixtures of activators may also be used. Suitable compounds include organoaluminium compounds, organoboron compounds, organic salts, such as methyllithium and methylmagnesium bromide, inorganic acids and salts, such as tetrafluoroboric acid etherate, silver tetrafluoroborate, sodium hexafluoroahtimonate and the like. Suitable organoaluminium compounds include compounds of the formula AIR 3 , where each R is independently a C C 12 alkyl, an oxygen containing moiety or a halide, and compounds such as LiAIH 4 and the like.
- Examples include trimethylaluminium (TMA), triethylaluminium (TEA), tri-isobutylaluminium (TIBA), tri-n-octylaluminium, methylaluminium dichloride, ethylaluminium dichloride, dimethylaluminium chloride, diethylaluminium chloride, aluminium isopropoxide, ethylaluminiumsesquichloride, methylaluminiumsesquichloride, and aluminoxanes.
- Aluminoxanes are well known in the art as typically oligomeric compounds which can be prepared by the controlled addition of water to an alkylaluminium compound, for example trimethylaluminium. Such . compounds can be linear, cyclic, cages or mixtures thereof. Mixtures of different aluminoxanes may also be used in the process.
- organoboron compounds examples include boroxines, NaBH 4 , triethylborane, tris(pentafluoropheny)borane, tributyl borate and the like.
- the activator may also be or contain a compound that acts as a reducing or oxidising agent, such as sodium or zinc metal and the like, or oxygen and the like.
- the activator may be selected from alkylaluminoxanes such as methylaluminoxane (MAO) and ethylaluminoxane (EAO) as well as modified alkylaluminoxanes such as modified methylaluminoxane (MMAO).
- alkylaluminoxanes such as methylaluminoxane (MAO) and ethylaluminoxane (EAO)
- modified alkylaluminoxanes such as modified methylaluminoxane (MMAO).
- Modified methylaluminoxane (a commercial product from Akzo Nobel) contains modifier groups such as isobutyl or n-octyl groups, in addition to methyl groups.
- the transition metal and the aluminoxane may be combined in proportions to provide Al/metal ratios from about 1 :1 to 10 000:1, preferably from about 1 :1 to 1000:1 , and more preferably from 1 :1 to 300:1.
- the process may include the step of adding to the catalyst system a trialkylaluminium compound in amounts of between 0.01 to 1000 mol per mol of alkylaluminoxane.
- aluminoxanes generally also contain considerable quantities of the corresponding trialkylaluminium compounds used in their preparation. The presence of these trialkylaluminium compounds in aluminoxanes can be attributed to their incomplete hydrolysis with water. Any quantity of a trialkylaluminium compound quoted in this disclosure is additional to alkylaluminium compounds contained within the aluminoxanes.
- the process may include the step of mixing the components of the catalyst system at any temperature between -20°C and 250°C in the presence of an olefin.
- an olefin may stabilise the catalyst system.
- the individual components of the catalyst system described herein may be combined simultaneously or sequentially in any order, and in the presence or absence of a solvent, in order to give an active catalyst.
- the mixing of the catalyst components can be conducted at any temperature between -20°C and 250°C.
- the presence of an olefin during the mixing of the catalyst components generally provides a protective effect which may result in improved catalyst performance.
- the preferred temperature range may be between 20°C and 100°C.
- the catalyst system in accordance with the invention, or its individual components, may also be immobilised by supporting it on a support material, for example, silica, alumina, MgCI 2 , zirconia or mixtures thereof, or on a polymer, for example polyethylene, polypropylene, polystyrene, or poly(aminostyrene).
- a support material for example, silica, alumina, MgCI 2 , zirconia or mixtures thereof, or on a polymer, for example polyethylene, polypropylene, polystyrene, or poly(aminostyrene).
- the catalyst can be formed in situ in the presence of the support material, or the support can be pre-impregnated or premixed, simultaneously or sequentially, with one or more of the catalyst components.
- the support material can also act as a component of the activator. This approach would also facilitate the recovery of the catalyst from the reaction mixture for reuse.
- the support can also act as a catalyst component, for example where such supports contain aluminoxane functionalities or where the support is capable of performing similar, chemical functions as an aluminoxane, which is for instance the case with IOLATM (a commercial product from Grace Davison).
- reaction products or in other words olefin oligomers, as described herein may be prepared using the disclosed catalyst system by homogeneous liquid phase reaction in the presence or absence of an inert solvent, and/or by slurry reaction where the catalyst system is in a form that displays little or no solubility, and/or a two-phase liquid/liquid reaction, and/or a bulk phase reaction in which neat reagent and/or product olefins serve as the dominant medium, and/or gas phase reaction, using conventional equipment and contacting techniques.
- the process may therefore also be carried out in an inert solvent.
- Any inert solvent that does not react with the activator can be used.
- These inert solvents may include any saturated aliphatic and unsaturated aliphatic and aromatic hydrocarbon and halogenated hydrocarbon.
- Typical solvents include, but are not limited to, benzene, toluene, xylene, cumene, heptane, methylcyclohexane, methylcyclopentane, cyclohexane, 1-hexene, 1- octene, ionic liquids and the like.
- the process may be carried out at pressures from atmospheric to 500 barg. Ethylene pressures in the range of 10-70 barg are preferred. Particularly preferred pressures range from 30-50 barg.
- the process may be carried out at temperatures from - 20 °C - 250 °C. Temperatures in the range of 15-130 °C are preferred. Particularly preferred temperatures range from 35- 100°C.
- the heteroatomic coordination complex and reaction conditions are selected such that the yield of 1 -octene from ethylene is greater than 30 mass %, preferably greater than 35 mass %.
- yield refers to grams of 1 -octene formed per 100g of total reaction product formed.
- the process may also yield different quantities of 1-butene, 1- hexene, methylcyclopentane, methylene cyclopentane, propylcyclopentane, propylene cyclopentane and specific higher oligomers, depending on the nature of the heteroatomic ligand and the reaction conditions.
- a number of these products cannot be formed via conventional ethylene oligomerisation and trimerisation technologies in the yields observed in the present invention.
- the catalyst, its individual components, reagents, solvents and reaction products are generally employed on a once-through basis, any of these materials can, and are indeed preferred to be recycled to some extent in order to minimise production costs.
- the process may be carried out in a plant which includes any type of reactor.
- reactors include, but are not limited to, batch reactors, semi-batch reactors and continuous reactors.
- the plant may include, in combination a) a reactor, b) at least one inlet line into this reactor for olefin reactant and the catalyst system, c) effluent lines from this reactor for oligomerisation reaction products, and d) at least one separator to separate the desired oligomerisation reaction products, wherein the catalyst system may include a heteroatomic coordination complex of a transition metal compound and an activator, as described herein.
- the reactor and a separator may be combined to facilitate the simultaneous formation of reaction products and separation of these compounds from the reactor.
- This process principle is commonly known as reactive distillation.
- the catalyst system exhibits no solubility in the solvent or reaction products, and is fixed in the reactor so that it does not exit the reactor with the reactor product, solvent and unreacted olefin, the process principle is commonly known as catalytic distillation.
- a catalyst system for the tetramerisation of olefins.
- the catalyst system may include a heteroatomic ligand as described above and a transition metal.
- the catalyst system may also include an activator as described above.
- the heteroatomic ligand may be described by the following general formula (R) n A-B-C(R) m where A and C are independently selected from a group which comprises phosphorus, arsenic, antimony, oxygen, bismuth, sulphur, selenium, and nitrogen, and B is a linking group between A and C, and R is independently selected from any homo or heterohydrocarbyl group of which at least one R group is substituted with a polar substituent and n and m is determined by the respective valence and oxidation state of A and C.
- a and/or C may be a potential electron donor for coordination with the transition metal.
- An electron donor or electron donating substituent is defined as that entity that donates electrons used in chemical, including dative covalent, bond formation.
- the heteroatomic ligand may be described by the following general formula (R 1 )(R 2 )A-B- C(R 3 )(R 4 ) where A and C are independently selected from a group which comprises phosphorus, arsenic, antimony, bismuth and nitrogen and B is a linking group between A and C, and R 1 , R 2 , R 3 and R 4 are independently selected from non-aromatic and aromatic, including heteroaromatic, groups of which at least one of R 1 , R 2 , R 3 and R 4 is substituted with a polar substituent.
- each of R 1 , R 2 , R 3 and R 4 may be aromatic, including heteroaromatic, but preferably not all of R 1 , R 2 , R 3 and R 4 , if they all are aromatic, are substituted by any substituent on an atom adjacent to the atom bound to A or C.
- R 1 , R 2 , R 3 and R 4 may have substituents on the atom adjacent to the atom bound to A or C.
- Any polar substituents on R 1 , R 2 , R 3 and R 4 may preferably not be on the atom adjacent to the atom bound to A or C.
- Any polar substituent on one or more of R 1 , R 2 , R 3 and R 4 may be electron donating.
- Polar is defined as an entity with a permanent electric dipole moment.
- Polar substituents include methoxy, ethoxy, isopropoxy, C 3 -C 20 alkoxy, phenoxy, pentafluorophenoxy, trimethylsiloxy, dimethylamino, methylsulfanyl, tosyl, methoxymethy, methylthiomethyl, 1 ,3-oxazolyl, methomethoxy, hydroxyl, amino, phosphino, arsino, stibino, sulphate, nitro and the like.
- Any of the groups R 1 , R 2 , R 3 and R 4 may independently be linked to one or more of each other or to the linking group B to form a cyclic structure together with A and C, A and B or B and C.
- R 1 , R 2 , R 3 and R 4 may be independently selected from a group comprising a benzyl, phenyl, tolyl, xylyl, mesityl, biphenyl, naphthyl, anthracenyl, methoxy, ethoxy, phenoxy, tolyloxy, dimethylamino, diethylamino, methylethylamino, thiophenyl, pyridyl, thioethyl, thiophenoxy, trimethylsilyl, dimethylhydrazyl, methyl, ethyl, ethenyl, propyl, butyl, propenyl, propynyl, cyclopentyl, cyclohexyl, ferrocenyl and tetrahydrofuranyl group.
- R 1 , R 2 , R 3 and R 4 may independently be selected from a group comprising a phenyl, tolyl,
- a and/or C may be independently oxidised by S, Se, N or O, where the valence of A and/or C allows for such oxidation.
- a and C may be independently phosphorus or phosphorus oxidised by S or Se or N or O.
- B may be selected from any one of a group comprising: organic linking groups comprising a hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl and a substituted heterohydrocarbyl; inorganic linking groups comprising single atom links; ionic links; and a group comprising methylene, dimethylmethylene, 1 ,2-ethane, 1 ,2-phenylene, 1 ,2- propane, 1 ,2-catechol, 1 ,2-dimethylhydrazine, -B(R 5 )-, -Si(R 5 ) 2 -, -P(R 5 )- and -N(R 5 )- where R 5 is hydrogen, a hydrocarbyl or substituted hydrocarbyl, a substituted heteroatom or a halogen.
- B may be -N(R 5 )- and R 5 is a hydrocarbyl or a substituted hydrocarbyl group.
- R 5 may be hydrogen or may be selected from the groups consisting of alkyl, substituted alkyl, aryl, substituted aryl, aryloxy, substituted aryloxy, halogen, nitro, alkoxycarbonyl, carbonyloxy, alkoxy, aminocarbonyl, carbonylamino, dialkylamino, silyl groups or derivatives thereof, and aryl substituted with any of these substituents.
- R 5 may be an isopropyl, a 1-cyclohexylethyl, a 2- methylcyclohexyl or a 2-octyl group.
- a single atom linking spacer is defined as a substituted or non-substituted atom that is bound directly to A and C.
- the ligand may also contain multiple (R) n A-B-C(R) m units. Not limiting examples of such ligands include dendrimeric ligands as well as ligands where the individual units are coupled either via one or more of the R groups or via the linking group B .
- examples of such ligands may include 1 ,2-di-(N(P(4-phenyl) 2 ) 2 )- benzene, 1 ,4-di-(N(P(4-methoxyphenyl) 2 ) 2 )-benzene, N(CH 2 CH 2 N(P(4- methoxyphenyl) 2 ) 2 ) 3 and 1 ,4-di-(P(4-methoxyphenyl)N(methyl)P(4-methoxyphenyl) 2 )- benzene.
- ligands can be prepared using procedures known to one skilled in the art and procedures disclosed in published literature. Examples of ligands are: (3- methoxyphenyl) 2 PN(methyl)P(3-methoxyphenyl) 2 , (4-methoxyphenyl) 2 PN(methyl)P(4- methoxyphenyl) 2 , (3-methoxyphenyl) 2 PN(isopropyl)P(3-methoxyphenyl) 2 ,(4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 , (4-methoxyphenyl) 2 PN(2- ethylhexyl)P(4-methoxyphenyl) 2 , (3-methoxyphenyl)(phenyl)PN(methyl)P(phenyl) 2 and (4-methoxyphenyl)(phenyl)PN(methyl)P(phenyl) 2 , (3- methoxypheny
- the transition metal may be selected from any one of a group comprising chromium, molybdenum, tungsten, titanium, tantalum, vanadium and zirconium, preferably chromium.
- the transition metal may be derived from a transition metal compound selected from a simple inorganic or organic salt, a co-ordination or organometallic complex, which may be selected from a group comprising chromium trichloride tris-tetrahydrofuran complex, (benzene)tricarbonyl chromium, chromium (III) octanoate, chromium (III) acetylacetonoate, chromium hexacarbonyl, and chromium (III) 2-ethylhexanoate.
- the preferred transition metal compounds include chromium (III) acetylacetonoate and chromium (III) 2-ethylhexanoate.
- the transition metal compound and heteroatomic ligand may have metal/ligand ratios from about 0.01 : 100 to 10 000:1, preferably from about 0.1 :1 to 10:1.
- the catalyst system may also include an activator as described above.
- the activator may in principle be any compound that generates an active catalyst when combined with the heteroatomic ligand and the transition metal compound. Mixtures of activators may also be used. Suitable compounds include organoaluminium compounds, organoboron compounds, organic salts, such as methyl lithium and methylmagnesium bromide, inorganic acids and salts, such as tetrafluoroboric acid etherate, silver tetrafluoroborate, sodium hexafluoroantimonate and the like.
- the activator may be selected from alkylaluminoxanes such as methylaluminoxane (MAO) and ethylaluminoxane (EAO) as well as modified alkylaluminoxanes such as modified methylaluminoxane (MMAO).
- alkylaluminoxanes such as methylaluminoxane (MAO) and ethylaluminoxane (EAO)
- modified alkylaluminoxanes such as modified methylaluminoxane (MMAO).
- Modified methylaluminoxane (a commercial product from Akzo Nobel) contains modifier groups such as isobutyl or n-octyl groups, in addition to methyl groups.
- the transition metal and the aluminoxane may be in such proportions relative to each other to provide Al/metal ratios from about 1 :1 to 10 000:1 , preferably from about 1 :1 to 1000:1 , and more preferably from 1 :1
- the catalyst system may also include a trialkylaluminium compound in amounts of between 0.01 to 100 mol per mol of aluminoxane.
- a ligand as described above, for a catalyst system, as described above, for the tetramerisation of olefins.
- the invention also extends to the identification and use of ligands suitable for use in a tetramerisation of olefins process or catalyst system.
- EAO ethylaluminoxane
- 72.042 g/mol corresponding to the (CH 3 CH 2 -AI-O) building block
- modified methylaluminoxane prepared from a 70:30 mixture of trimethylaluminium and tri- isobutylaluminium as 70.7 g/mol corresponding to the (Me 0 . 70 isonBu 0 . 3 o-AI-O) unit.
- Ethylene oligomerisation products were analysed by GC-MS and GC-FID.
- the mixed heteroatomic PNP ligands were made by reacting amines and phosphine chlorides R 2 PCI as described in (a) Ewart et al, J. Chem. Soc. 1964, 1543; (b) Dossett, S.J. et al, Chem. Commun., 2001, 8, 699; (c) Balakrishna, M.S. et al, J. Organomet. Chem. 1990, 390, 2, 203).
- the respective phosphine chlorides R 2 PCI were prepared as described in literature (Casalnuovo, A.L. er a/, J. Am. Chem. Soc. 1994, 116, 22, 9869; Rajanbabu, TN.
- the Grignard reagent was added to N,N-diisopropylphosphoramide dichloride (6.64 ml, 36 mmol) in THF (100 ml) at 0 ° C. After stirring at room temperature overnight the mixture was diluted with cyclohexane (200 ml) and dry HCI gas was bubbled through the solution for 0.5 hours. After filtration of the precipitate, the solvent was removed to give a mixture of the phosphine chloride and bromide in an 80% yield. This crude product was not isolated and all was used in the next step.
- Example 2 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(methyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 65°C, while the ethylene pressure was kept at 30 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 30 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 3 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (3- methoxyphenyl) 2 PN(methyl)P(3-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 65°C, while the ethylene pressure was kept at 30 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 30 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 4 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 65°C, while the ethylene pressure was kept at 30 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 30 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 5 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 12 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 6 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 11 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC-FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 7 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 21 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 8 Ethylene tetramerisation reaction using CrCI 3 .THF 3 , (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 30 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC-FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 9 Ethylene tetramerisation reaction using Cr (III) 2-ethylhexanoate , (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 30 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 10 Ethylene tetramerisation reaction using Cr (III) octanoanoate , (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 40 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC-FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 11 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 30 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 12 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 15 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 13 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MMAO-3A
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 22 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC-FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC-FID.
- Example 14 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and EAO/TMA
- the mixture was stirred for 5 min at ambient temperature and was then transferred to a 300 ml pressure reactor (autoclave) containing a mixture of toluene (80ml), EAO (ethylaluminoxane in toluene, 33 mmol) and TMA (trimethylaluminium, 8.25mmol) at 40°C.
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer.
- the reaction was terminated after 60 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C.
- Example 15 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (4- methoxyphenyl) 2 PN(isopropyl)P(4-methoxyphenyl) 2 and MAO in the presence of
- the pressure reactor was first charged with hydrogen to a pressure of approximately 2.5 barg and subsequently with ethylene to 45 barg after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 15 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC- FID.
- Example 16 Ethylene tetramerisation reaction using Cr (III) acetylacetonoate, (phenyl)2PN(isopropyl)P(2-methoxyphenyl) 2 and MAO
- the pressure reactor was first charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was kept at 45 barg. Thorough mixing was ensured throughout by mixing speeds of 1100 RPM's using a gas entraining stirrer. The reaction was terminated after 15 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 10°C. After releasing the excess ethylene from the autoclave, the liquid contained in the autoclave was quenched with ethanol followed by 10% hydrochloric acid in water. Nonane was added as an internal standard for the analysis of the liquid phase by GC-FID. A small sample of the organic layer was dried over anhydrous sodium sulfate and then analysed by GC- FID.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
Description
Claims
Priority Applications (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/539,237 US7297832B2 (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
AT03813853T ATE477053T1 (en) | 2002-12-20 | 2003-12-19 | TETRAMERIZATION OF OLEFINS |
AU2003297545A AU2003297545A1 (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
CNB2003801091309A CN100548947C (en) | 2002-12-20 | 2003-12-19 | Four of alkene gathers |
BRPI0317516A BRPI0317516B1 (en) | 2002-12-20 | 2003-12-19 | olefin tetramerization |
BR0317516-2A BR0317516A (en) | 2002-12-20 | 2003-12-19 | Olefin tetramerization |
JP2005511968A JP2006511625A (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
DE60333790T DE60333790D1 (en) | 2002-12-20 | 2003-12-19 | TETRAMERIZATION OF OLEFINES |
EP03813853A EP1578531B9 (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
CA2510801A CA2510801C (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
Applications Claiming Priority (12)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US43540502P | 2002-12-20 | 2002-12-20 | |
US60/435,405 | 2002-12-20 | ||
ZA200210339 | 2002-12-20 | ||
ZA2002/10339 | 2002-12-20 | ||
US47837903P | 2003-06-13 | 2003-06-13 | |
US60/478,379 | 2003-06-13 | ||
ZA200304632 | 2003-06-13 | ||
ZA2003/4632 | 2003-06-13 | ||
US50930903P | 2003-10-06 | 2003-10-06 | |
ZA200307774 | 2003-10-06 | ||
ZA2003/7774 | 2003-10-06 | ||
US60/509,309 | 2003-10-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004056478A1 true WO2004056478A1 (en) | 2004-07-08 |
Family
ID=32686408
Family Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/ZA2003/000186 WO2004056478A1 (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
PCT/ZA2003/000185 WO2004056477A1 (en) | 2002-12-20 | 2003-12-19 | Trimerisation of olefins |
PCT/ZA2003/000187 WO2004056479A1 (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
Family Applications After (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/ZA2003/000185 WO2004056477A1 (en) | 2002-12-20 | 2003-12-19 | Trimerisation of olefins |
PCT/ZA2003/000187 WO2004056479A1 (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
Country Status (13)
Country | Link |
---|---|
US (1) | US7511183B2 (en) |
EP (3) | EP1581342B1 (en) |
JP (2) | JP2006516265A (en) |
KR (3) | KR20060002742A (en) |
CN (3) | CN100548946C (en) |
AT (2) | ATE477053T1 (en) |
AU (3) | AU2003297546A1 (en) |
BR (6) | BR0317516A (en) |
CA (3) | CA2510190C (en) |
DE (1) | DE60331252D1 (en) |
ES (1) | ES2340483T3 (en) |
PL (3) | PL377211A1 (en) |
WO (3) | WO2004056478A1 (en) |
Cited By (74)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005123633A1 (en) * | 2004-06-18 | 2005-12-29 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds in an aliphatic medium |
WO2006108803A1 (en) * | 2005-04-08 | 2006-10-19 | Shell Internationale Research Maatschappij B.V. | Catalytic trimerization and tetramerization of olefinic monomers |
US7129304B1 (en) | 2005-07-21 | 2006-10-31 | Chevron Phillips Chemical Company Lp | Dimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
WO2007007272A2 (en) | 2005-07-12 | 2007-01-18 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds in the presence of a diluted metal containing activator |
JP2007056002A (en) * | 2005-07-27 | 2007-03-08 | Sumitomo Chemical Co Ltd | Method for producing olefin oligomer |
US7268096B2 (en) | 2005-07-21 | 2007-09-11 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
US7271121B2 (en) | 2005-07-21 | 2007-09-18 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
US7273959B2 (en) | 2003-10-10 | 2007-09-25 | Shell Oil Company | Catalytic trimerization of olefinic monomers |
US7378537B2 (en) | 2006-07-25 | 2008-05-27 | Chevron Phillips Chemical Company Lp | Olefin oligomerization catalysts and methods of using same |
WO2008119153A1 (en) | 2007-03-29 | 2008-10-09 | Nova Chemicals (International) S.A. | Amino phosphine |
JP2009516580A (en) * | 2005-11-21 | 2009-04-23 | シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー | Catalytic oligomerization of olefin monomers |
US7687672B2 (en) | 2006-02-03 | 2010-03-30 | Exxonmobil Chemical Patents Inc. | In-line process for generating comonomer |
US7727926B2 (en) | 2005-07-21 | 2010-06-01 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and method of using in oligomerization and polymerization |
US20100190939A1 (en) * | 2007-07-11 | 2010-07-29 | Fritz Peter M | Catalyst composition and process for di-, tri-and/or tetramerization of ethylene |
WO2010092554A1 (en) | 2009-02-16 | 2010-08-19 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds in the presence of an activated oligomerisation catalyst |
US7786336B2 (en) | 2006-03-10 | 2010-08-31 | Petrochina Company Limited | Catalyst composition for ethylene oligomerization and the use thereof |
US7820581B2 (en) | 2004-02-20 | 2010-10-26 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
US7858833B2 (en) | 2006-02-03 | 2010-12-28 | Exxonmobil Chemical Patents Inc. | Process for generating linear alpha olefin comonomers |
US7902415B2 (en) | 2007-12-21 | 2011-03-08 | Chevron Phillips Chemical Company Lp | Processes for dimerizing or isomerizing olefins |
US7910670B2 (en) | 2005-08-19 | 2011-03-22 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
WO2011045701A1 (en) | 2009-10-16 | 2011-04-21 | Sasol Technology (Proprietary) Limited | Separation of components from a multi-component hydrocarbon stream which includes ethylene |
WO2011048527A1 (en) | 2009-10-19 | 2011-04-28 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds with reduced polymer formation |
WO2011085951A1 (en) | 2010-01-15 | 2011-07-21 | Basell Polyolefine Gmbh | Oligomerization of olefins |
US7994376B2 (en) | 2004-02-19 | 2011-08-09 | Chevron Phillips Chemical Company Lp | Olefin oligomerization |
CN102164935A (en) * | 2008-09-29 | 2011-08-24 | 诺瓦化学品(国际)股份有限公司 | Ethylene trimerization catalysts comprising P-N-P ligands and their use |
US8067609B2 (en) | 2007-01-08 | 2011-11-29 | Exxonmobil Chemical Patents Inc. | Methods for oligomerizing olefins with chromium pyridine thioether catalysts |
US8076523B2 (en) | 2004-06-18 | 2011-12-13 | Sasol Technology (Pty) Limited | Oligomerisation in the presence of both a tetramerisation catalyst and a further oligomerisation catalyst |
US8138348B2 (en) | 2007-01-08 | 2012-03-20 | Exxonmobil Chemical Patents Inc. | Methods for oligomerizing olefins with chromium pyridine mono-oxazoline catalysts |
WO2012055943A2 (en) | 2010-10-28 | 2012-05-03 | Basell Polyolefine Gmbh | Oligomerization of olefins |
US8211949B2 (en) | 2007-09-24 | 2012-07-03 | Dow Global Technologies Llc | Functionalized long-chain olefin mixtures and uses therefor |
US8227653B2 (en) | 2009-03-27 | 2012-07-24 | Exxonmobil Chemical Patents Inc. | Olefin oligomerization reaction processes exhibiting reduced fouling |
US8252874B2 (en) | 2006-12-22 | 2012-08-28 | Shell Oil Company | Ligands and catalyst systems for the oligomerization of olefinic monomers |
RU2461423C2 (en) * | 2007-01-18 | 2012-09-20 | ЭсКей ЭНЕРДЖИ КО., ЛТД. | Catalyst systems for tetramerisation of ethylene and method of producing 1-octene using said catalyst systems |
US8329608B2 (en) | 2004-02-20 | 2012-12-11 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
US8404915B2 (en) * | 2006-08-30 | 2013-03-26 | Exxonmobil Chemical Patents Inc. | Phosphine ligand-metal compositions, complexes, and catalysts for ethylene trimerizations |
WO2013110170A1 (en) | 2012-01-25 | 2013-08-01 | Nova Chemicals (International) S.A. | P-n-p ligand |
WO2013168099A1 (en) | 2012-05-09 | 2013-11-14 | Sasol Technology (Proprietary) Limited | A process for oligomerising a hydrocarbon to form at least one co-monomer product |
WO2013168103A1 (en) | 2012-05-09 | 2013-11-14 | Sasol Technology (Proprietary) Limited | Oligomerisation of olefinic compounds with reduced polymer formation |
WO2013168098A1 (en) | 2012-05-09 | 2013-11-14 | Sasol Technology (Proprietary) Limited | Separation of components from a multi-component hydrocarbon stream |
US8629280B2 (en) | 2007-01-08 | 2014-01-14 | Exxonmobil Chemical Patents Inc. | Methods for oligomerizing olefins with chromium pyridine ether catalysts |
US8778827B2 (en) | 2007-11-28 | 2014-07-15 | Saudi Basic Industries Corporation | Catalyst composition and process for oligomerization of ethylene |
CN104059105A (en) * | 2013-03-20 | 2014-09-24 | 中国石油化工股份有限公司 | Ligand compound containing pyridyl group, and catalyst containing ligand compound and application thereof |
US8962903B2 (en) | 2010-10-06 | 2015-02-24 | Nova Chemicals (International) S.A. | Tetramerization ligands |
WO2015083053A1 (en) | 2013-12-05 | 2015-06-11 | Nova Chemicals (International) S.A. | Ethylene oligomerization with mixed ligands |
WO2015097599A1 (en) | 2013-12-23 | 2015-07-02 | Nova Chemicals (International) S.A. | Continuous ethylene oligomerization with in-situ catalyst preparation |
US9375709B2 (en) | 2012-03-16 | 2016-06-28 | Sk Innovation Co., Ltd. | Catalyst systems for preparing 1-hexene and/or 1-octene from ethylene |
US9487456B2 (en) | 2012-05-09 | 2016-11-08 | Sasol Technology (Proprietary) Limited | Tetramerisation of ethylene |
US9499456B2 (en) | 2012-05-09 | 2016-11-22 | Sasol Technology (Proprietary) Limited | Tetramerisation of ethylene |
US9550841B2 (en) | 2004-02-20 | 2017-01-24 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
US9586872B2 (en) | 2011-12-30 | 2017-03-07 | Chevron Phillips Chemical Company Lp | Olefin oligomerization methods |
US9688588B2 (en) | 2012-12-21 | 2017-06-27 | Nova Chemicals (International) S.A. | Continuous ethylene tetramerization process |
WO2018012792A1 (en) | 2016-07-14 | 2018-01-18 | Sk Innovation Co., Ltd. | Oligomerization of ethylene |
KR20180008268A (en) | 2016-07-14 | 2018-01-24 | 에스케이이노베이션 주식회사 | Oligomerisation of ethylene |
US9944661B2 (en) | 2016-08-09 | 2018-04-17 | Chevron Phillips Chemical Company Lp | Olefin hydroboration |
EP3214087A4 (en) * | 2015-10-21 | 2018-07-18 | LG Chem, Ltd. | Ligand compound, catalyst system for olefin oligomerization, and olefin oligomerization method using same |
US10160696B2 (en) | 2010-12-01 | 2018-12-25 | Nova Chemicals (International) S.A. | Heat management in ethylene oligomerization |
US10183960B1 (en) | 2017-09-22 | 2019-01-22 | Chevron Phillips Chemical Company Lp | Perfluorohydrocarbyl-N2-phosphinyl amidine compounds, chromium salt complexes, catalyst systems, and their use to oligomerize ethylene |
US10232339B2 (en) | 2017-06-06 | 2019-03-19 | Chevron Phillips Chemical Company Lp | Fouling protection for an oligomerization reactor inlet |
US10294171B2 (en) | 2017-09-22 | 2019-05-21 | Chevron Phillips Chemical Company Lp | Carbonyl-containing perfluorohydrocarbyl-N2-phosphinyl amidine compounds, chromium salt complexes and their use to oligomerize ethylene |
US10329212B2 (en) | 2016-05-27 | 2019-06-25 | Chevron Phillips Chemical Company Lp | Reduced polymer formation for selective ethylene oligomerizations |
US10392451B2 (en) | 2015-06-12 | 2019-08-27 | Lg Chem, Ltd. | Ligand compound, organic chromium compound, catalyst system for olefin oligomerization, and method for oligomerizing olefins using the same thereof |
US10414699B2 (en) | 2016-05-27 | 2019-09-17 | Chevron Phillips Chemical Company Lp | Process improvements in selective ethylene oligomerizations |
US10414698B2 (en) | 2016-05-27 | 2019-09-17 | Chevron Phillips Chemical Company Lp | Reduced polymer formation for selective ethylene oligomerizations |
US10464862B2 (en) | 2017-09-28 | 2019-11-05 | Chevron Phillips Chemical Company Lp | Oligomerization reactions using aluminoxanes |
US10493442B2 (en) | 2017-09-22 | 2019-12-03 | Chevron Phillips Chemical Company Lp | Fluorinated N2-phosphinyl amidine compounds, chromium salt complexes, catalyst systems, and their use to oligomerize ethylene |
WO2020147373A1 (en) | 2019-01-15 | 2020-07-23 | 中国石油化工股份有限公司 | Halogen-containing compound and use thereof, catalyst composition, and ethylene oligomerization, trimerization and tetramerization methods |
WO2020147372A1 (en) | 2019-01-15 | 2020-07-23 | 中国石油化工股份有限公司 | Halogen-containing compound and use thereof as catalyst ligand in ethylene oligomerization |
FR3116738A1 (en) | 2020-11-30 | 2022-06-03 | IFP Energies Nouvelles | NEW CATALYTIC COMPOSITION BASED ON CHROMIUM COMPRISING AN AROMATIC ETHER ADDITIVE AND ASSOCIATED PROCESS FOR THE OLIGOMERIZATION OF ETHYLENE INTO OCTENE-1 |
FR3116739A1 (en) | 2020-11-30 | 2022-06-03 | IFP Energies Nouvelles | NEW CATALYTIC COMPOSITION BASED ON CHROME COMPRISING AN AROMATIC HYDROCARBON ADDITIVE AND ASSOCIATED METHOD FOR THE OLIGOMERIZATION OF ETHYLENE INTO OCTENE-1 |
US11492305B1 (en) | 2021-11-08 | 2022-11-08 | Chevron Phillips Chemical Company, Lp | Chromium phosphinyl hydroisoindole amidine complexes for tetramerization of ethylene |
US11505513B1 (en) | 2021-11-08 | 2022-11-22 | Chevron Phillips Chemical Company, Lp | Chromium bicyclic phosphinyl amidine complexes for tetramerization of ethylene |
US11583843B1 (en) | 2021-11-08 | 2023-02-21 | Chevron Phillips Chemical Company, Lp | Chromium phosphinyl isoindole amidine complexes for tetramerization of ethylene |
FR3128710A1 (en) | 2021-11-02 | 2023-05-05 | IFP Energies Nouvelles | Ethylene oligomerization process using a catalytic composition comprising a chromium precursor, a PNP type ligand and an aluminoxane |
FR3140775A1 (en) | 2022-10-17 | 2024-04-19 | IFP Energies Nouvelles | New catalytic composition based on supported chromium or titanium |
Families Citing this family (129)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4982952B2 (en) * | 2005-02-14 | 2012-07-25 | 住友化学株式会社 | Ethylene trimerization catalyst and ethylene trimerization method using the catalyst |
JP2006218437A (en) * | 2005-02-14 | 2006-08-24 | Sumitomo Chemical Co Ltd | Trimerization catalyst of olefin and trimerization method of olefin using it |
EP1871729B1 (en) * | 2005-03-09 | 2014-01-15 | ExxonMobil Chemical Patents Inc. | Methods for oligomerizing olefins |
US7414006B2 (en) * | 2005-03-09 | 2008-08-19 | Exxonmobil Chemical Patents Inc. | Methods for oligomerizing olefins |
US7323611B2 (en) | 2005-06-28 | 2008-01-29 | Sumitomo Chemical Company Limited | Process for producing olefin oligomer |
JP2007039641A (en) * | 2005-06-28 | 2007-02-15 | Sumitomo Chemical Co Ltd | Method for producing olefin oligomer |
US7550639B2 (en) | 2005-07-27 | 2009-06-23 | Sumitomo Chemical Company, Limited | Process for producing olefin oligomer |
GB0520085D0 (en) * | 2005-10-03 | 2005-11-09 | Sasol Tech Pty Ltd | Oligomerisation of olefinic compounds in the presence of an oligomerisation catalyst, and a catalyst activator including a halogenated -AR group |
US8874477B2 (en) | 2005-10-04 | 2014-10-28 | Steven Mark Hoffberg | Multifactorial optimization system and method |
KR20080080570A (en) * | 2005-11-21 | 2008-09-04 | 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 | Catalytic process for the oligomerization of olefinic monomers |
US8003839B2 (en) * | 2006-02-03 | 2011-08-23 | Exxonmobil Chemical Patents Inc. | Process for generating linear apha olefin comonomers |
US7982085B2 (en) * | 2006-02-03 | 2011-07-19 | Exxonmobil Chemical Patents Inc. | In-line process for generating comonomer |
WO2007092136A2 (en) | 2006-02-03 | 2007-08-16 | Exxonmobil Chemical Patents, Inc. | Process for generating alpha olefin comonomers |
EP1991353A1 (en) * | 2006-02-03 | 2008-11-19 | Ineos Europe Limited | Transition metal catalysts |
CN101600723A (en) | 2006-12-22 | 2009-12-09 | 国际壳牌研究有限公司 | The part and the catalyst system thereof that are used for catalytic oligomerization of olefinic monomers |
KR101095796B1 (en) * | 2007-02-08 | 2011-12-21 | 에스케이종합화학 주식회사 | Ethylene Tetramerization Catalytst Systems for Immobilization and Process Using the Same |
JP4974732B2 (en) * | 2007-03-30 | 2012-07-11 | 三井化学株式会社 | Method for producing cyclic olefin |
WO2008146215A1 (en) * | 2007-05-28 | 2008-12-04 | Sasol Technology (Pty) Limited | Two stage activation of oligomerisation catalyst and oligomerisation of olefinic compounds in the presence of an oligomerisation catalyst so activated |
KR101057576B1 (en) * | 2007-08-16 | 2011-08-17 | 에스케이종합화학 주식회사 | Selective Ethylene Oligomerization Catalyst System |
JP2009072665A (en) * | 2007-09-19 | 2009-04-09 | Mitsui Chemicals Inc | Catalyst for olefin polymerization, and manufacturing method of ethylene polymer |
CA2705155C (en) | 2007-11-07 | 2015-12-29 | Sasol Technology (Proprietary) Limited | Process for polymerising or oligomerising a hydrocarbon |
EP2217551B1 (en) | 2007-11-07 | 2014-06-04 | Sasol Technology (Proprietary) Limited | Process for polymerising or oligomerising a hydrocarbon |
ES2367133T3 (en) | 2008-04-04 | 2011-10-28 | Saudi Basic Industries Corporation | CATALYST FOR THE OLIGOMERIZATION OF ETHYLENE, PROCEDURE FOR THE PREPARATION OF THE SAME AND PROCEDURE OF OLIGOMERIZATION THAT USES THE SAME. |
JP5208870B2 (en) * | 2008-07-11 | 2013-06-12 | 三井化学株式会社 | Method for producing silylated polyolefin and additive containing silylated polyolefin |
CA2639882C (en) * | 2008-09-29 | 2016-07-12 | Nova Chemicals Corporation | Tetramerization |
KR101065596B1 (en) * | 2009-01-29 | 2011-09-19 | 에스케이종합화학 주식회사 | High Active and High Selective Ethylene Oligomerization Catalyst, and process for preparing hexene or octene using thereof |
EP2239056B1 (en) | 2009-04-09 | 2011-07-20 | Saudi Basic Industries Corporation | Catalyst composition and process for oligomerization of ethylene |
CN102107146B (en) * | 2009-12-29 | 2013-10-16 | 中国石油天然气股份有限公司 | Catalyst for synthesizing hexene-1 by ethylene trimerization and application thereof |
CA2785473C (en) | 2009-12-31 | 2023-01-10 | Chevron Phillips Chemical Company Lp | Phosphinyl amidine compounds, metal complexes, catalyst systems, and their use to oligomerize or polymerize olefins |
CN102781948A (en) | 2010-02-12 | 2012-11-14 | 埃南蒂亚有限公司 | Enantiomerically enriched aminodiphosphines as ligands for the preparation of catalysts for asymmetric synthesis |
CN102282179B (en) * | 2010-03-03 | 2013-11-06 | Sk新技术 | Highly active and highly selective ethylene oligomerization catalyst, and preparation method of hexene or octene using same |
CA2703435C (en) * | 2010-05-12 | 2017-05-02 | Nova Chemicals Corporation | Oligomerization process using a chromium p-n-p catalyst with added alkyl zinc |
EP2489431B1 (en) | 2011-02-16 | 2013-05-01 | Linde AG | Method for preparing a catalyst composition for oligomerization of ethylene and respective catalyst composition pre-formation unit |
RU2470707C1 (en) * | 2011-06-27 | 2012-12-27 | Общество с ограниченной ответственностью "Объединенный центр исследований и разработок" | Catalyst for trimerisation of ethylene to 1-hexene, ligand for producing catalyst, method of producing catalyst and method of producing ligand |
JP5844636B2 (en) | 2011-12-27 | 2016-01-20 | 出光興産株式会社 | Method for producing α-olefin |
US9133079B2 (en) | 2012-01-13 | 2015-09-15 | Siluria Technologies, Inc. | Process for separating hydrocarbon compounds |
CA2874526C (en) | 2012-05-24 | 2022-01-18 | Siluria Technologies, Inc. | Oxidative coupling of methane systems and methods |
US8865610B2 (en) | 2012-06-06 | 2014-10-21 | Chevron Phillips Chemical Company Lp | Phosphinyl guanidine compounds, metal salt complexes, catalyst systems, and their use to oligomerize or polymerize olefins |
US9670113B2 (en) | 2012-07-09 | 2017-06-06 | Siluria Technologies, Inc. | Natural gas processing and systems |
KR101483248B1 (en) * | 2012-11-15 | 2015-01-16 | 주식회사 엘지화학 | Ligand compound, organic chromium compound, catalyst system for ethylene oligomerization, method for preparign the same, and method for ethylene oligomerization using the same |
WO2014089479A1 (en) | 2012-12-07 | 2014-06-12 | Siluria Technologies, Inc. | Integrated processes and systems for conversion of methane to multiple higher hydrocarbon products |
US9616421B2 (en) * | 2013-02-27 | 2017-04-11 | Mitsui Chemicals, Inc. | Catalyst for olefin multimerization and method for producing olefin multimer in presence of catalyst for olefin multimerization |
WO2014181248A1 (en) | 2013-05-09 | 2014-11-13 | Sasol Technology (Proprietary) Limited | Oligomerisation of ethylene to mixtures of 1-hexene and 1-octene |
CA2908559C (en) | 2013-05-09 | 2021-08-17 | Sasol Technology (Proprietary) Limited | Oligomerisation of ethylene to mixtures of 1-hexene and 1-octene |
CN105263890B (en) | 2013-05-09 | 2017-12-05 | 沙索技术有限公司 | Four poly- methods of ethene |
FR3007761B1 (en) * | 2013-06-28 | 2016-02-05 | IFP Energies Nouvelles | NEW NICKEL COMPLEX AND USE THEREOF IN OLEFIN OLIGOMERIZATION PROCESS |
EP2832445A1 (en) * | 2013-07-29 | 2015-02-04 | Linde AG | Catalyst composition and process for oligomerization of ethylene |
CN104415790B (en) * | 2013-08-23 | 2017-06-30 | 中国石油化工股份有限公司 | A kind of catalyst for ethylene tetramerization composition and application |
KR101599012B1 (en) * | 2013-11-18 | 2016-03-03 | 주식회사 엘지화학 | Ligand compound, catalyst system for olefin oligomerization, and method for olefin oligomerization using the same |
KR20150058034A (en) * | 2013-11-18 | 2015-05-28 | 주식회사 엘지화학 | Ligand compound, catalyst system for olefin oligomerization, and method for olefin oligomerization using the same |
KR101676835B1 (en) * | 2013-11-18 | 2016-11-17 | 주식회사 엘지화학 | Ligand compound, catalyst system for olefin oligomerization, and method for olefin oligomerization using the same |
KR101657259B1 (en) | 2013-11-19 | 2016-09-13 | 주식회사 엘지화학 | Ligand compound, catalyst system for olefin oligomerization, and method for olefin oligomerization using the same |
WO2015081122A2 (en) | 2013-11-27 | 2015-06-04 | Siluria Technologies, Inc. | Reactors and systems for oxidative coupling of methane |
EP3092286A4 (en) | 2014-01-08 | 2017-08-09 | Siluria Technologies, Inc. | Ethylene-to-liquids systems and methods |
AU2015204709B2 (en) | 2014-01-09 | 2019-08-15 | Lummus Technology Llc | Oxidative coupling of methane implementations for olefin production |
US10377682B2 (en) | 2014-01-09 | 2019-08-13 | Siluria Technologies, Inc. | Reactors and systems for oxidative coupling of methane |
CN112246285A (en) | 2014-02-03 | 2021-01-22 | 沙特基础工业公司 | Catalyst composition pre-forming unit for preparing a catalyst composition for the oligomerization of ethylene |
US9175109B1 (en) | 2014-05-20 | 2015-11-03 | Chevron Phillips Chemical Company Lp | Oligomerization processes and polymer compositions produced therefrom |
CN106164103B (en) * | 2014-06-18 | 2018-05-25 | 株式会社Lg化学 | Ligand compound, organo-chromium compound, the catalyst system for olefin oligomerization and the method for olefin oligomerization using the catalyst system |
BR112017001004A2 (en) * | 2014-07-24 | 2017-11-14 | Linde Ag | catalyst composition, process for ethylene oligomerization and ethylene oligomerization reaction which produces 1-hexene and 1-octene |
CN105562099B (en) * | 2014-10-08 | 2018-01-23 | 中国石油化工股份有限公司 | A kind of catalyst for ethylene tetramerization composition and ethylene tetramerization method |
CN105562098B (en) * | 2014-10-08 | 2018-03-02 | 中国石油化工股份有限公司 | A kind of ethylene oligomerisation catalyst composition and its application |
CN105566036B (en) * | 2014-10-13 | 2018-05-11 | 中国石油化工股份有限公司 | A kind of method of ethylene tetramerization |
JP6488638B2 (en) * | 2014-10-28 | 2019-03-27 | セントラル硝子株式会社 | Method for producing α-fluoroaldehyde equivalents |
WO2016105228A1 (en) * | 2014-12-23 | 2016-06-30 | Public Joint Stock Company "Sibur Holding" | Methods of preparing oligomers of an olefin |
MX369759B (en) * | 2015-01-19 | 2019-11-20 | Evonik Operations Gmbh | Combined preparation of butene and octene from ethene. |
US9505675B2 (en) | 2015-02-09 | 2016-11-29 | Chevron Phillips Chemical Company Lp | Deactivation of a process by-product |
KR101679515B1 (en) * | 2015-02-12 | 2016-11-24 | 주식회사 엘지화학 | Method of preparing catalyst system for oligomerization and catalyst sysyem for oligomerization prepared thereby |
WO2016149024A2 (en) * | 2015-03-13 | 2016-09-22 | Dow Global Technologies Llc | Chromium complex and catalyst therefrom |
US10793490B2 (en) | 2015-03-17 | 2020-10-06 | Lummus Technology Llc | Oxidative coupling of methane methods and systems |
US9334204B1 (en) | 2015-03-17 | 2016-05-10 | Siluria Technologies, Inc. | Efficient oxidative coupling of methane processes and systems |
US20160289143A1 (en) | 2015-04-01 | 2016-10-06 | Siluria Technologies, Inc. | Advanced oxidative coupling of methane |
KR101761395B1 (en) * | 2015-04-15 | 2017-07-25 | 주식회사 엘지화학 | Ligand compound, catalyst system for oligomerization, and method for olefin oligomerization using the same |
US10513474B2 (en) | 2015-05-15 | 2019-12-24 | Lg Chem, Ltd. | Catalyst composition and method of preparing polyolefin using the same |
KR20160134464A (en) | 2015-05-15 | 2016-11-23 | 주식회사 엘지화학 | Supported hybrid catalyst system and method for olefin polymerization using the same |
KR101768194B1 (en) * | 2015-05-15 | 2017-08-16 | 주식회사 엘지화학 | Catalyst composition and method for preparing polyolefin using the same |
KR101757370B1 (en) | 2015-06-01 | 2017-07-12 | 주식회사 엘지화학 | 1-Octene composition |
WO2016205411A2 (en) | 2015-06-16 | 2016-12-22 | Siluria Technologies, Inc. | Ethylene-to-liquids systems and methods |
US9328297B1 (en) | 2015-06-16 | 2016-05-03 | Siluria Technologies, Inc. | Ethylene-to-liquids systems and methods |
WO2017010998A1 (en) | 2015-07-14 | 2017-01-19 | Chevron Phillips Chemical Company Lp | Olefin compositions |
US9732300B2 (en) | 2015-07-23 | 2017-08-15 | Chevron Phillipa Chemical Company LP | Liquid propylene oligomers and methods of making same |
KR102058142B1 (en) * | 2015-09-02 | 2019-12-20 | 주식회사 엘지화학 | Ligand compound, catalyst system for olefin oligomerization, and method for olefin oligomerization using the same |
KR101749542B1 (en) | 2015-09-03 | 2017-06-21 | 한택규 | Process for selective oligomerization of Ethylene |
KR20170032766A (en) * | 2015-09-15 | 2017-03-23 | 주식회사 엘지화학 | Method for oligomerization of olefins |
CN108025996A (en) | 2015-09-16 | 2018-05-11 | 沙特基础工业全球技术有限公司 | Method for the inactivation of olefin oligomerization catalyst |
US10519077B2 (en) | 2015-09-18 | 2019-12-31 | Chevron Phillips Chemical Company Lp | Ethylene oligomerization/trimerization/tetramerization reactor |
US10513473B2 (en) | 2015-09-18 | 2019-12-24 | Chevron Phillips Chemical Company Lp | Ethylene oligomerization/trimerization/tetramerization reactor |
KR101735687B1 (en) * | 2015-09-23 | 2017-05-15 | 롯데케미칼 주식회사 | Catalyst system for olefin oligomerization, and method for olefin oligomerization using the same |
US20170107162A1 (en) | 2015-10-16 | 2017-04-20 | Siluria Technologies, Inc. | Separation methods and systems for oxidative coupling of methane |
CN105289742B (en) * | 2015-11-11 | 2018-07-13 | 天津科技大学 | For the catalyst of ethylene selectivity oligomerisation, ligand and preparation method thereof |
US20190322965A1 (en) | 2015-12-04 | 2019-10-24 | Sabic Global Technologies B.V. | Process for flushing an oligomerization reactor and oligomerization of an olefin |
CN108778479A (en) | 2016-03-21 | 2018-11-09 | 沙特基础工业全球技术有限公司 | Method for handling oligomerization product stream |
KR102222844B1 (en) * | 2016-03-22 | 2021-03-04 | 아파렌 테크놀로지 (자싱) | Catalyst for the production of novel linear alpha olefins, preparation and use thereof |
US9944573B2 (en) | 2016-04-13 | 2018-04-17 | Siluria Technologies, Inc. | Oxidative coupling of methane for olefin production |
WO2017187289A1 (en) | 2016-04-25 | 2017-11-02 | Sabic Global Technologies B.V. | Process for removing heat from an oligomerization reaction |
KR102545533B1 (en) | 2016-05-27 | 2023-06-21 | 에스케이이노베이션 주식회사 | Oligomerization Catalyst And Process For Preparing Ethylene Oligomer Using Thereof |
FR3051683B1 (en) | 2016-05-31 | 2020-10-09 | Ifp Energies Now | CATALYTIC COMPOSITION BASED ON CHROME AND A LIGAND BASED ON PHOSPHINE AND ITS USE IN A PROCESS FOR PROCESSING OCTENS |
CN106111200B (en) * | 2016-06-21 | 2019-03-12 | 东南大学 | More metal corsslinkings cooperation catalyst and its preparation method and application for uns-dimethylhydrazine degradation |
MX2019000598A (en) * | 2016-07-15 | 2019-06-13 | Sibur Holding Public Joint Stock Co | Method of oligomerization of olefins. |
CN106582851B (en) * | 2016-10-17 | 2019-04-30 | 天津科技大学 | Catalytic component and its catalyst for ethylene selectivity oligomerisation |
EP3536696A4 (en) | 2016-11-02 | 2020-03-11 | Ajou University Industry-Academic Cooperation Foundation | Chrome compound, catalyst system using same, and method for preparing ethylene oligomer |
WO2018118105A1 (en) | 2016-12-19 | 2018-06-28 | Siluria Technologies, Inc. | Methods and systems for performing chemical separations |
CN110099883A (en) | 2016-12-22 | 2019-08-06 | 沙特基础工业全球技术有限公司 | The method of production of linear alpha-olefins |
US20200122131A1 (en) | 2016-12-30 | 2020-04-23 | Sabic Global Technologies B.V. | Methods of Producing Linear Alpha Olefins |
EP3562585B1 (en) | 2016-12-30 | 2023-08-23 | SABIC Global Technologies B.V. | Method for preparation of homogenous catalyst for selective 1-hexene production |
US11285469B2 (en) | 2016-12-30 | 2022-03-29 | Sabic Global Technologies B.V. | Method for preparation of a catalyst solution for selective 1-hexene production |
KR20200034961A (en) | 2017-05-23 | 2020-04-01 | 루머스 테크놀로지 엘엘씨 | Integration of methane oxidative coupling process |
KR102450815B1 (en) | 2017-06-16 | 2022-10-05 | 에스케이이노베이션 주식회사 | Heteroatomic ligand, oligomerization catalyst containing the same, and production method of oligomer |
SG11202000016XA (en) | 2017-07-06 | 2020-01-30 | Mitsui Chemicals Inc | Catalyst for olefin multimerization and method for producing olefin multimer in presence of said catalyst |
WO2019010498A1 (en) | 2017-07-07 | 2019-01-10 | Siluria Technologies, Inc. | Systems and methods for the oxidative coupling of methane |
WO2019074303A1 (en) * | 2017-10-11 | 2019-04-18 | 롯데케미칼 주식회사 | Catalyst system for olefin oligomerization and method for preparing olefin oligomer by using same |
WO2019074304A1 (en) * | 2017-10-11 | 2019-04-18 | 롯데케미칼 주식회사 | Catalyst system for olefin oligomerization and method for preparing olefin oligomer by using same |
WO2019168249A1 (en) | 2018-02-27 | 2019-09-06 | 에스케이이노베이션 주식회사 | Ligand, oligomerization catalyst comprising same, and method for producing ethylene oligomer by using oligomerization catalyst |
KR102605188B1 (en) | 2018-02-27 | 2023-11-24 | 에스케이이노베이션 주식회사 | Ligand, Oligomerization Catalyst And Process For Preparing Ethylene Oligomer Using Thereof |
US11148127B2 (en) | 2018-06-07 | 2021-10-19 | Ajou University Industry-Academic Cooperation Foundation | Bisphosphine ligand compound, chromium compound, ethylene oligomerization catalyst system, and ethylene oligomer preparation method |
JP2020111570A (en) * | 2019-01-09 | 2020-07-27 | 三井化学株式会社 | Method for producing olefin polymer performed in the presence of catalyst for olefin polymerization |
WO2020185426A1 (en) | 2019-03-13 | 2020-09-17 | Tpc Group Llc | Flexible manufacturing system for selectively producing different linear alpha olefins |
FR3108264B1 (en) | 2020-03-19 | 2022-04-08 | Ifp Energies Now | Ethylene oligomerization plant to produce alpha-olefins |
CN112387311A (en) * | 2020-10-22 | 2021-02-23 | 杭州小菱科技有限公司 | Ethylene oligomerization catalyst system, preparation method and application thereof |
KR102631413B1 (en) | 2021-06-15 | 2024-01-31 | 한화토탈에너지스 주식회사 | Method for ethylene oligomerization |
KR20230027512A (en) | 2021-08-19 | 2023-02-28 | 에스케이이노베이션 주식회사 | Chromium catalyst precursors, ethylene oligomerization catalyst comprising the same and process for preparing ethylene oligomer |
CN113773430B (en) * | 2021-09-13 | 2023-01-13 | 万华化学集团股份有限公司 | Preparation method of alpha-olefin copolymer |
CN113996343A (en) * | 2021-11-19 | 2022-02-01 | 中化泉州石化有限公司 | Catalyst composition for preparing 1-octene |
CN116328839A (en) * | 2021-12-24 | 2023-06-27 | 中国石油化工股份有限公司 | Supported main catalyst for oligomerization of ethylene, catalyst composition for oligomerization of ethylene and application |
CN116328836B (en) * | 2021-12-24 | 2024-09-20 | 中国石油化工股份有限公司 | Porous organic polymer supported ethylene polymerization main catalyst, ethylene polymerization catalyst composition and application |
KR20230134435A (en) * | 2022-03-14 | 2023-09-21 | 주식회사 엘지화학 | Ligand compound, organic chromium compound and catalyst composition comprising the same |
CN115124575B (en) * | 2022-06-23 | 2024-02-27 | 中国五环工程有限公司 | Preparation method of PNP ligand structure Cr (III) metal catalyst |
US11639321B1 (en) | 2022-08-31 | 2023-05-02 | Saudi Arabian Oil Company | Catalyst systems that include meta-alkoxy substituted n-aryl bis-diphosphinoamine ligands |
US11623901B1 (en) | 2022-08-31 | 2023-04-11 | Saudi Arabian Oil Company | Catalyst systems that include silyl ether moieties |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2699457A (en) * | 1950-06-21 | 1955-01-11 | Ziegler Karl | Polymerization of ethylene |
US4628138A (en) * | 1985-09-20 | 1986-12-09 | Ashland Oil, Inc. | Catalyst and process for oligomerization of ethylene |
WO2002004119A1 (en) * | 2000-07-11 | 2002-01-17 | Bp Chemicals Limited | Olefin trimerisation using a catalyst comprising a source of chromium, molybdenum or tungsten and a ligand containing at least one phosphorous, arsenic or antimony atom bound to at least one (hetero)hydrocarbyl group |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1020563A (en) | 1961-11-21 | 1966-02-23 | Gulf Research Development Co | Process for polymerizing ethylene |
US3635937A (en) | 1969-11-05 | 1972-01-18 | Shell Oil Co | Ethylene polymerization |
US3676523A (en) | 1971-07-16 | 1972-07-11 | Shell Oil Co | Alpha-olefin production |
US3906053A (en) | 1971-08-10 | 1975-09-16 | Ethyl Corp | Process for the production of olefins |
JPH07215896A (en) * | 1994-02-04 | 1995-08-15 | Idemitsu Kosan Co Ltd | Production of alpha-olefin oligomer |
JPH09143228A (en) * | 1995-11-22 | 1997-06-03 | Sumitomo Chem Co Ltd | Production of ethylene/alpha-olefin copolymer |
US6184428B1 (en) | 1998-04-22 | 2001-02-06 | Saudi Basic Industries Corporation | Catalyst and process for ethylene oligomerization |
GB9918635D0 (en) * | 1999-08-06 | 1999-10-13 | Bp Chem Int Ltd | Polymerisation process |
AU2002359912A1 (en) | 2001-12-20 | 2003-07-09 | Sasol Technology (Pty) Ltd. | Trimerisation and oligomerisation of olefins using a chromium based catalyst |
-
2003
- 2003-12-19 EP EP03813854A patent/EP1581342B1/en not_active Expired - Lifetime
- 2003-12-19 BR BR0317516-2A patent/BR0317516A/en not_active IP Right Cessation
- 2003-12-19 JP JP2005511967A patent/JP2006516265A/en not_active Withdrawn
- 2003-12-19 CN CNB2003801091277A patent/CN100548946C/en not_active Expired - Lifetime
- 2003-12-19 EP EP03813853A patent/EP1578531B9/en not_active Expired - Lifetime
- 2003-12-19 BR BR0317510-3A patent/BR0317510A/en active IP Right Grant
- 2003-12-19 DE DE60331252T patent/DE60331252D1/en not_active Expired - Lifetime
- 2003-12-19 ES ES03813852T patent/ES2340483T3/en not_active Expired - Lifetime
- 2003-12-19 BR BRPI0316870-0A patent/BRPI0316870B1/en unknown
- 2003-12-19 AU AU2003297546A patent/AU2003297546A1/en not_active Abandoned
- 2003-12-19 CN CNB2003801091332A patent/CN100540514C/en not_active Expired - Lifetime
- 2003-12-19 PL PL377211A patent/PL377211A1/en not_active Application Discontinuation
- 2003-12-19 BR BR0316870-0A patent/BR0316870A/en active IP Right Grant
- 2003-12-19 WO PCT/ZA2003/000186 patent/WO2004056478A1/en active Application Filing
- 2003-12-19 PL PL377488A patent/PL377488A1/en not_active Application Discontinuation
- 2003-12-19 KR KR1020057011608A patent/KR20060002742A/en not_active Application Discontinuation
- 2003-12-19 BR BRPI0317516A patent/BRPI0317516B1/en unknown
- 2003-12-19 AU AU2003297545A patent/AU2003297545A1/en not_active Abandoned
- 2003-12-19 EP EP03813852A patent/EP1581341B1/en not_active Expired - Lifetime
- 2003-12-19 PL PL377406A patent/PL377406A1/en not_active Application Discontinuation
- 2003-12-19 AT AT03813853T patent/ATE477053T1/en not_active IP Right Cessation
- 2003-12-19 BR BRPI0317510-3A patent/BRPI0317510B1/en unknown
- 2003-12-19 WO PCT/ZA2003/000185 patent/WO2004056477A1/en active Application Filing
- 2003-12-19 CA CA2510190A patent/CA2510190C/en not_active Expired - Lifetime
- 2003-12-19 KR KR1020057011604A patent/KR20050100600A/en not_active Application Discontinuation
- 2003-12-19 AU AU2003297544A patent/AU2003297544A1/en not_active Abandoned
- 2003-12-19 US US10/539,517 patent/US7511183B2/en not_active Expired - Lifetime
- 2003-12-19 CA CA2510194A patent/CA2510194C/en not_active Expired - Lifetime
- 2003-12-19 CA CA2510801A patent/CA2510801C/en not_active Expired - Lifetime
- 2003-12-19 AT AT03813852T patent/ATE457196T1/en not_active IP Right Cessation
- 2003-12-19 CN CNB2003801091309A patent/CN100548947C/en not_active Expired - Lifetime
- 2003-12-19 KR KR1020057011601A patent/KR20060002741A/en not_active Application Discontinuation
- 2003-12-19 WO PCT/ZA2003/000187 patent/WO2004056479A1/en active Application Filing
- 2003-12-19 JP JP2005511969A patent/JP2006517528A/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2699457A (en) * | 1950-06-21 | 1955-01-11 | Ziegler Karl | Polymerization of ethylene |
US4628138A (en) * | 1985-09-20 | 1986-12-09 | Ashland Oil, Inc. | Catalyst and process for oligomerization of ethylene |
WO2002004119A1 (en) * | 2000-07-11 | 2002-01-17 | Bp Chemicals Limited | Olefin trimerisation using a catalyst comprising a source of chromium, molybdenum or tungsten and a ligand containing at least one phosphorous, arsenic or antimony atom bound to at least one (hetero)hydrocarbyl group |
Non-Patent Citations (6)
Title |
---|
ANTHEA CARTER, STEVEN COHEN, NEIL COOLEY, ADEN MURPHY, JAMES SCUTT, DUNAN WASS: "High activity ethylene trimerisation catalysts based on diphosphine ligands", CHEMICAL COMMUNICATION, vol. 2002, no. 8, 20 March 2002 (2002-03-20), pages 858 - 859, XP002277009 * |
BALAKRISHNA, M.S. ET AL., J. ORGANOMET. CHEM., vol. 390, no. 2, 1990, pages 203 |
CASALNUOVO, A.L. ET AL., J. AM. CHEM. SOC., vol. 116, no. 22, 1994, pages 9869 |
DOSSETT, S.J., CHEM. COMMUN., vol. 8, 2001, pages 699 |
EWART ET AL., J. CHEM. SOC., 1964, pages 1543 |
RAJANBABU, T.V. ET AL., J. ORG. CHEM., vol. 62, no. 17, 1997, pages 6012 |
Cited By (104)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7273959B2 (en) | 2003-10-10 | 2007-09-25 | Shell Oil Company | Catalytic trimerization of olefinic monomers |
US7994376B2 (en) | 2004-02-19 | 2011-08-09 | Chevron Phillips Chemical Company Lp | Olefin oligomerization |
US9550841B2 (en) | 2004-02-20 | 2017-01-24 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
US8329608B2 (en) | 2004-02-20 | 2012-12-11 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
US8993822B2 (en) | 2004-02-20 | 2015-03-31 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
US7820581B2 (en) | 2004-02-20 | 2010-10-26 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
US8076523B2 (en) | 2004-06-18 | 2011-12-13 | Sasol Technology (Pty) Limited | Oligomerisation in the presence of both a tetramerisation catalyst and a further oligomerisation catalyst |
US7964763B2 (en) | 2004-06-18 | 2011-06-21 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds in an aliphatic medium |
WO2005123633A1 (en) * | 2004-06-18 | 2005-12-29 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds in an aliphatic medium |
US7381857B2 (en) | 2005-04-08 | 2008-06-03 | Shell Oil Company | Catalytic trimerization and tetramerization of olefinic monomers |
US7259123B2 (en) | 2005-04-08 | 2007-08-21 | Shell Oil Company | Catalytic trimerization and tetramerization of olefinic monomers |
WO2006108803A1 (en) * | 2005-04-08 | 2006-10-19 | Shell Internationale Research Maatschappij B.V. | Catalytic trimerization and tetramerization of olefinic monomers |
EP1915329B2 (en) † | 2005-07-12 | 2016-05-11 | Sasol Technology (Pty) Ltd | Oligomerisation of olefinic compounds in the presence of a diluted metal containing activator |
WO2007007272A2 (en) | 2005-07-12 | 2007-01-18 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds in the presence of a diluted metal containing activator |
US7728161B2 (en) | 2005-07-21 | 2010-06-01 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
US7268096B2 (en) | 2005-07-21 | 2007-09-11 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
US7727926B2 (en) | 2005-07-21 | 2010-06-01 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and method of using in oligomerization and polymerization |
US7129304B1 (en) | 2005-07-21 | 2006-10-31 | Chevron Phillips Chemical Company Lp | Dimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
US7728160B2 (en) | 2005-07-21 | 2010-06-01 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
US7271121B2 (en) | 2005-07-21 | 2007-09-18 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
US7977269B2 (en) | 2005-07-21 | 2011-07-12 | Chevron Phillips Chemical Company Lp | Diimine metal complexes, methods of synthesis, and methods of using in oligomerization and polymerization |
JP2007056002A (en) * | 2005-07-27 | 2007-03-08 | Sumitomo Chemical Co Ltd | Method for producing olefin oligomer |
US7910670B2 (en) | 2005-08-19 | 2011-03-22 | Chevron Phillips Chemical Company Lp | Methods of preparation of an olefin oligomerization catalyst |
JP2009516580A (en) * | 2005-11-21 | 2009-04-23 | シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー | Catalytic oligomerization of olefin monomers |
US7867938B2 (en) * | 2005-11-21 | 2011-01-11 | Shell Oil Company | Catalytic oligomerization of olefinic monomers |
US7687672B2 (en) | 2006-02-03 | 2010-03-30 | Exxonmobil Chemical Patents Inc. | In-line process for generating comonomer |
US7858833B2 (en) | 2006-02-03 | 2010-12-28 | Exxonmobil Chemical Patents Inc. | Process for generating linear alpha olefin comonomers |
US7786336B2 (en) | 2006-03-10 | 2010-08-31 | Petrochina Company Limited | Catalyst composition for ethylene oligomerization and the use thereof |
EP2289901A1 (en) * | 2006-07-25 | 2011-03-02 | Chevron Phillips Chemical Company LP | Olefin oligomerization catalysts and methods of using same |
CN101511851B (en) * | 2006-07-25 | 2015-04-15 | 切夫里昂菲利普化学有限责任公司 | Olefin oligomerization catalysts and methods of using same |
EP2287172A1 (en) * | 2006-07-25 | 2011-02-23 | Chevron Phillips Chemical Company LP | Olefin oligomerization catalysts and methods of using same |
US7378537B2 (en) | 2006-07-25 | 2008-05-27 | Chevron Phillips Chemical Company Lp | Olefin oligomerization catalysts and methods of using same |
US8334420B2 (en) | 2006-07-25 | 2012-12-18 | Chevron Phillips Chemical Company Lp | Olefin oligomerization catalysts and methods of using same |
US8404915B2 (en) * | 2006-08-30 | 2013-03-26 | Exxonmobil Chemical Patents Inc. | Phosphine ligand-metal compositions, complexes, and catalysts for ethylene trimerizations |
US8476181B2 (en) | 2006-12-22 | 2013-07-02 | Shell Oil Company | Catalyst systems for the oligomerization of olefin monomers |
US8252874B2 (en) | 2006-12-22 | 2012-08-28 | Shell Oil Company | Ligands and catalyst systems for the oligomerization of olefinic monomers |
US8629280B2 (en) | 2007-01-08 | 2014-01-14 | Exxonmobil Chemical Patents Inc. | Methods for oligomerizing olefins with chromium pyridine ether catalysts |
US8067609B2 (en) | 2007-01-08 | 2011-11-29 | Exxonmobil Chemical Patents Inc. | Methods for oligomerizing olefins with chromium pyridine thioether catalysts |
US8138348B2 (en) | 2007-01-08 | 2012-03-20 | Exxonmobil Chemical Patents Inc. | Methods for oligomerizing olefins with chromium pyridine mono-oxazoline catalysts |
RU2461423C2 (en) * | 2007-01-18 | 2012-09-20 | ЭсКей ЭНЕРДЖИ КО., ЛТД. | Catalyst systems for tetramerisation of ethylene and method of producing 1-octene using said catalyst systems |
WO2008119153A1 (en) | 2007-03-29 | 2008-10-09 | Nova Chemicals (International) S.A. | Amino phosphine |
US8252956B2 (en) | 2007-03-29 | 2012-08-28 | Nova Chemicals (International) S.A. | Amino phosphine |
US7994363B2 (en) | 2007-03-29 | 2011-08-09 | Nova Chemicals (International) S.A | Amino phosphine |
US8637721B2 (en) * | 2007-07-11 | 2014-01-28 | Saudi Basic Industries Corporation | Catalyst composition and process for di-, tri- and/or tetramerization of ethylene |
US20100190939A1 (en) * | 2007-07-11 | 2010-07-29 | Fritz Peter M | Catalyst composition and process for di-, tri-and/or tetramerization of ethylene |
US8211949B2 (en) | 2007-09-24 | 2012-07-03 | Dow Global Technologies Llc | Functionalized long-chain olefin mixtures and uses therefor |
US8778827B2 (en) | 2007-11-28 | 2014-07-15 | Saudi Basic Industries Corporation | Catalyst composition and process for oligomerization of ethylene |
US7902415B2 (en) | 2007-12-21 | 2011-03-08 | Chevron Phillips Chemical Company Lp | Processes for dimerizing or isomerizing olefins |
CN102164935A (en) * | 2008-09-29 | 2011-08-24 | 诺瓦化学品(国际)股份有限公司 | Ethylene trimerization catalysts comprising P-N-P ligands and their use |
WO2010092554A1 (en) | 2009-02-16 | 2010-08-19 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds in the presence of an activated oligomerisation catalyst |
US8227653B2 (en) | 2009-03-27 | 2012-07-24 | Exxonmobil Chemical Patents Inc. | Olefin oligomerization reaction processes exhibiting reduced fouling |
WO2011045701A1 (en) | 2009-10-16 | 2011-04-21 | Sasol Technology (Proprietary) Limited | Separation of components from a multi-component hydrocarbon stream which includes ethylene |
WO2011048527A1 (en) | 2009-10-19 | 2011-04-28 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds with reduced polymer formation |
US8859696B2 (en) | 2009-10-19 | 2014-10-14 | Sasol Technology (Pty) Limited | Oligomerisation of olefinic compounds with reduced polymer formation |
WO2011085951A1 (en) | 2010-01-15 | 2011-07-21 | Basell Polyolefine Gmbh | Oligomerization of olefins |
US8962903B2 (en) | 2010-10-06 | 2015-02-24 | Nova Chemicals (International) S.A. | Tetramerization ligands |
WO2012055943A2 (en) | 2010-10-28 | 2012-05-03 | Basell Polyolefine Gmbh | Oligomerization of olefins |
US10160696B2 (en) | 2010-12-01 | 2018-12-25 | Nova Chemicals (International) S.A. | Heat management in ethylene oligomerization |
US9586872B2 (en) | 2011-12-30 | 2017-03-07 | Chevron Phillips Chemical Company Lp | Olefin oligomerization methods |
WO2013110170A1 (en) | 2012-01-25 | 2013-08-01 | Nova Chemicals (International) S.A. | P-n-p ligand |
US9375709B2 (en) | 2012-03-16 | 2016-06-28 | Sk Innovation Co., Ltd. | Catalyst systems for preparing 1-hexene and/or 1-octene from ethylene |
US9499456B2 (en) | 2012-05-09 | 2016-11-22 | Sasol Technology (Proprietary) Limited | Tetramerisation of ethylene |
WO2013168098A1 (en) | 2012-05-09 | 2013-11-14 | Sasol Technology (Proprietary) Limited | Separation of components from a multi-component hydrocarbon stream |
WO2013168103A1 (en) | 2012-05-09 | 2013-11-14 | Sasol Technology (Proprietary) Limited | Oligomerisation of olefinic compounds with reduced polymer formation |
US9399179B2 (en) | 2012-05-09 | 2016-07-26 | Sasol Technology Proprietary Limited | Separation of components from a multi-component hydrocarbon stream |
US9487456B2 (en) | 2012-05-09 | 2016-11-08 | Sasol Technology (Proprietary) Limited | Tetramerisation of ethylene |
WO2013168099A1 (en) | 2012-05-09 | 2013-11-14 | Sasol Technology (Proprietary) Limited | A process for oligomerising a hydrocarbon to form at least one co-monomer product |
US9688588B2 (en) | 2012-12-21 | 2017-06-27 | Nova Chemicals (International) S.A. | Continuous ethylene tetramerization process |
CN104059105A (en) * | 2013-03-20 | 2014-09-24 | 中国石油化工股份有限公司 | Ligand compound containing pyridyl group, and catalyst containing ligand compound and application thereof |
WO2015083053A1 (en) | 2013-12-05 | 2015-06-11 | Nova Chemicals (International) S.A. | Ethylene oligomerization with mixed ligands |
WO2015097599A1 (en) | 2013-12-23 | 2015-07-02 | Nova Chemicals (International) S.A. | Continuous ethylene oligomerization with in-situ catalyst preparation |
US10343152B2 (en) | 2013-12-23 | 2019-07-09 | Nova Chemicals (International) S.A. | Continuous ethylene oligomerization with in-situ catalyst preparation |
US10392451B2 (en) | 2015-06-12 | 2019-08-27 | Lg Chem, Ltd. | Ligand compound, organic chromium compound, catalyst system for olefin oligomerization, and method for oligomerizing olefins using the same thereof |
US10287373B2 (en) | 2015-10-21 | 2019-05-14 | Lg Chem, Ltd. | Ligand compound, catalyst system for olefin oligomerization, and method for oligomerizing olefins using the same |
EP3214087A4 (en) * | 2015-10-21 | 2018-07-18 | LG Chem, Ltd. | Ligand compound, catalyst system for olefin oligomerization, and olefin oligomerization method using same |
US10774015B2 (en) | 2016-05-27 | 2020-09-15 | Chevron Phillips Chemical Company Lp | Reduced polymer formation for selective ethylene oligomerizations |
US10689312B2 (en) | 2016-05-27 | 2020-06-23 | Chevron Phillip Chemical Company, LP | Process improvements in selective ethylene oligomerizations |
US10329212B2 (en) | 2016-05-27 | 2019-06-25 | Chevron Phillips Chemical Company Lp | Reduced polymer formation for selective ethylene oligomerizations |
US10414699B2 (en) | 2016-05-27 | 2019-09-17 | Chevron Phillips Chemical Company Lp | Process improvements in selective ethylene oligomerizations |
US10414698B2 (en) | 2016-05-27 | 2019-09-17 | Chevron Phillips Chemical Company Lp | Reduced polymer formation for selective ethylene oligomerizations |
US10689311B2 (en) | 2016-05-27 | 2020-06-23 | Chevron Phillips Chemical Company, Lp | Reduced polymer formation for selective ethylene oligomerizations |
US10919819B2 (en) | 2016-07-14 | 2021-02-16 | Sk Innovation Co., Ltd. | Oligomerization of ethylene |
KR20180008269A (en) | 2016-07-14 | 2018-01-24 | 에스케이이노베이션 주식회사 | Oligomerisation of ethylene |
KR20180008268A (en) | 2016-07-14 | 2018-01-24 | 에스케이이노베이션 주식회사 | Oligomerisation of ethylene |
WO2018012792A1 (en) | 2016-07-14 | 2018-01-18 | Sk Innovation Co., Ltd. | Oligomerization of ethylene |
US9944661B2 (en) | 2016-08-09 | 2018-04-17 | Chevron Phillips Chemical Company Lp | Olefin hydroboration |
US10232339B2 (en) | 2017-06-06 | 2019-03-19 | Chevron Phillips Chemical Company Lp | Fouling protection for an oligomerization reactor inlet |
US10493422B2 (en) | 2017-06-06 | 2019-12-03 | Chevron Phillips Chemical Company Lp | Fouling protection for an oligomerization reactor inlet |
US10294171B2 (en) | 2017-09-22 | 2019-05-21 | Chevron Phillips Chemical Company Lp | Carbonyl-containing perfluorohydrocarbyl-N2-phosphinyl amidine compounds, chromium salt complexes and their use to oligomerize ethylene |
US10183960B1 (en) | 2017-09-22 | 2019-01-22 | Chevron Phillips Chemical Company Lp | Perfluorohydrocarbyl-N2-phosphinyl amidine compounds, chromium salt complexes, catalyst systems, and their use to oligomerize ethylene |
US10493442B2 (en) | 2017-09-22 | 2019-12-03 | Chevron Phillips Chemical Company Lp | Fluorinated N2-phosphinyl amidine compounds, chromium salt complexes, catalyst systems, and their use to oligomerize ethylene |
US10464862B2 (en) | 2017-09-28 | 2019-11-05 | Chevron Phillips Chemical Company Lp | Oligomerization reactions using aluminoxanes |
US11826743B2 (en) | 2019-01-15 | 2023-11-28 | China Petroleum & Chemical Corporation | Halogen-containing compound and use thereof as catalyst ligand in ethylene oligomerization |
WO2020147373A1 (en) | 2019-01-15 | 2020-07-23 | 中国石油化工股份有限公司 | Halogen-containing compound and use thereof, catalyst composition, and ethylene oligomerization, trimerization and tetramerization methods |
WO2020147372A1 (en) | 2019-01-15 | 2020-07-23 | 中国石油化工股份有限公司 | Halogen-containing compound and use thereof as catalyst ligand in ethylene oligomerization |
US11306040B2 (en) | 2019-01-15 | 2022-04-19 | China Petroleum & Chemical Corporation | Halogen-containing compound and use thereof, catalyst composition, and ethylene oligomerization, trimerization and tetramerization methods |
FR3116738A1 (en) | 2020-11-30 | 2022-06-03 | IFP Energies Nouvelles | NEW CATALYTIC COMPOSITION BASED ON CHROMIUM COMPRISING AN AROMATIC ETHER ADDITIVE AND ASSOCIATED PROCESS FOR THE OLIGOMERIZATION OF ETHYLENE INTO OCTENE-1 |
FR3116739A1 (en) | 2020-11-30 | 2022-06-03 | IFP Energies Nouvelles | NEW CATALYTIC COMPOSITION BASED ON CHROME COMPRISING AN AROMATIC HYDROCARBON ADDITIVE AND ASSOCIATED METHOD FOR THE OLIGOMERIZATION OF ETHYLENE INTO OCTENE-1 |
FR3128710A1 (en) | 2021-11-02 | 2023-05-05 | IFP Energies Nouvelles | Ethylene oligomerization process using a catalytic composition comprising a chromium precursor, a PNP type ligand and an aluminoxane |
US11492305B1 (en) | 2021-11-08 | 2022-11-08 | Chevron Phillips Chemical Company, Lp | Chromium phosphinyl hydroisoindole amidine complexes for tetramerization of ethylene |
US11505513B1 (en) | 2021-11-08 | 2022-11-22 | Chevron Phillips Chemical Company, Lp | Chromium bicyclic phosphinyl amidine complexes for tetramerization of ethylene |
US11583843B1 (en) | 2021-11-08 | 2023-02-21 | Chevron Phillips Chemical Company, Lp | Chromium phosphinyl isoindole amidine complexes for tetramerization of ethylene |
FR3140775A1 (en) | 2022-10-17 | 2024-04-19 | IFP Energies Nouvelles | New catalytic composition based on supported chromium or titanium |
WO2024083616A1 (en) | 2022-10-17 | 2024-04-25 | IFP Energies Nouvelles | Novel chromium- or titanium-based supported catalytic composition |
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7297832B2 (en) | Tetramerization of olefins | |
CA2510801C (en) | Tetramerization of olefins | |
US7525009B2 (en) | Trimerisation of olefins | |
CA2570056C (en) | Oligomerisation in the presence of both a tetramerisation catalyst and a further oligomerisation catalyst | |
CA2570054C (en) | Oligomerisation of olefinic compounds in an aliphatic medium | |
US20090306442A1 (en) | Oligomerisation catalyst with pendant donor groups | |
WO2007039851A2 (en) | Oligomerisation of olefinic compounds in the presence of an oligomerisation catalyst, and a catalyst activator including a halogenated organic group | |
JP2006511625A (en) | Tetramerization of olefins | |
ES2350468T3 (en) | OLEFIN TRETRAMERIZATION. | |
ZA200504749B (en) | Tetramerization of olefins | |
ZA200504706B (en) | Trimerisation of olefins | |
ZA200504750B (en) | Tetramerization of olefins |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): BW GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2005/04750 Country of ref document: ZA Ref document number: 200504750 Country of ref document: ZA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2510801 Country of ref document: CA Ref document number: 2681/DELNP/2005 Country of ref document: IN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 377406 Country of ref document: PL Ref document number: 1020057011604 Country of ref document: KR Ref document number: 2003297545 Country of ref document: AU Ref document number: 2005511968 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2003813853 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: 2005122962 Country of ref document: RU Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 20038A91309 Country of ref document: CN |
|
WWP | Wipo information: published in national office |
Ref document number: 1020057011604 Country of ref document: KR |
|
ENP | Entry into the national phase |
Ref document number: PI0317516 Country of ref document: BR |
|
ENP | Entry into the national phase |
Ref document number: 2006173226 Country of ref document: US Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 10539237 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 10539237 Country of ref document: US |