WO2004056477A1 - Trimerisation of olefins - Google Patents
Trimerisation of olefins Download PDFInfo
- Publication number
- WO2004056477A1 WO2004056477A1 PCT/ZA2003/000185 ZA0300185W WO2004056477A1 WO 2004056477 A1 WO2004056477 A1 WO 2004056477A1 ZA 0300185 W ZA0300185 W ZA 0300185W WO 2004056477 A1 WO2004056477 A1 WO 2004056477A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- ethylphenyl
- catalyst system
- group
- transition metal
- methyl
- Prior art date
Links
- 150000001336 alkenes Chemical class 0.000 title claims abstract description 34
- 239000003054 catalyst Substances 0.000 claims abstract description 92
- 238000000034 method Methods 0.000 claims abstract description 86
- 239000003446 ligand Substances 0.000 claims abstract description 80
- 150000003623 transition metal compounds Chemical class 0.000 claims abstract description 37
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000013638 trimer Substances 0.000 claims abstract description 5
- -1 methylene, dimethylmethylene Chemical group 0.000 claims description 194
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 85
- 239000005977 Ethylene Substances 0.000 claims description 85
- CPOFMOWDMVWCLF-UHFFFAOYSA-N methyl(oxo)alumane Chemical compound C[Al]=O CPOFMOWDMVWCLF-UHFFFAOYSA-N 0.000 claims description 53
- 125000004429 atom Chemical group 0.000 claims description 49
- 125000001424 substituent group Chemical group 0.000 claims description 44
- 239000011651 chromium Substances 0.000 claims description 40
- 239000000203 mixture Substances 0.000 claims description 40
- 125000001183 hydrocarbyl group Chemical group 0.000 claims description 38
- 125000003118 aryl group Chemical group 0.000 claims description 36
- 238000002156 mixing Methods 0.000 claims description 32
- 239000011541 reaction mixture Substances 0.000 claims description 32
- 150000001875 compounds Chemical class 0.000 claims description 24
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 23
- 239000012190 activator Substances 0.000 claims description 23
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 22
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 21
- 229910052698 phosphorus Inorganic materials 0.000 claims description 21
- 239000011574 phosphorus Substances 0.000 claims description 21
- 125000005647 linker group Chemical group 0.000 claims description 20
- 229910052723 transition metal Inorganic materials 0.000 claims description 20
- 150000003624 transition metals Chemical class 0.000 claims description 20
- 229910052804 chromium Inorganic materials 0.000 claims description 19
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 18
- 125000001072 heteroaryl group Chemical group 0.000 claims description 16
- 229910052757 nitrogen Inorganic materials 0.000 claims description 15
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 claims description 14
- 229910052751 metal Inorganic materials 0.000 claims description 14
- 239000002184 metal Substances 0.000 claims description 14
- YVSMQHYREUQGRX-UHFFFAOYSA-N 2-ethyloxaluminane Chemical compound CC[Al]1CCCCO1 YVSMQHYREUQGRX-UHFFFAOYSA-N 0.000 claims description 13
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 13
- 229910052736 halogen Chemical group 0.000 claims description 12
- 150000002367 halogens Chemical group 0.000 claims description 12
- 125000005842 heteroatom Chemical group 0.000 claims description 12
- 239000001257 hydrogen Substances 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- 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 10
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 claims description 10
- 229910052785 arsenic Inorganic materials 0.000 claims description 10
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims description 10
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims description 10
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 10
- 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
- 229910052711 selenium Inorganic materials 0.000 claims description 9
- 239000011669 selenium Substances 0.000 claims description 9
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 8
- 125000001624 naphthyl group Chemical group 0.000 claims description 8
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 claims description 8
- 229910052717 sulfur Inorganic materials 0.000 claims description 8
- 125000003944 tolyl group Chemical group 0.000 claims description 8
- 125000000217 alkyl group Chemical group 0.000 claims description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 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
- 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 6
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 6
- 239000005864 Sulphur Substances 0.000 claims description 6
- 125000004104 aryloxy group Chemical group 0.000 claims description 6
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 claims description 6
- 239000004305 biphenyl Substances 0.000 claims description 6
- 235000010290 biphenyl Nutrition 0.000 claims description 6
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 6
- BFGKITSFLPAWGI-UHFFFAOYSA-N chromium(3+) Chemical compound [Cr+3] BFGKITSFLPAWGI-UHFFFAOYSA-N 0.000 claims description 6
- 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 6
- 229910052750 molybdenum Inorganic materials 0.000 claims description 6
- 239000011733 molybdenum Substances 0.000 claims description 6
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 125000004368 propenyl group Chemical group C(=CC)* 0.000 claims description 6
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 6
- 125000002568 propynyl group Chemical group [*]C#CC([H])([H])[H] 0.000 claims description 6
- 125000005023 xylyl group Chemical group 0.000 claims description 6
- OBETXYAYXDNJHR-UHFFFAOYSA-N 2-Ethylhexanoic acid Chemical compound CCCCC(CC)C(O)=O OBETXYAYXDNJHR-UHFFFAOYSA-N 0.000 claims description 5
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 claims description 5
- SHZIWNPUGXLXDT-UHFFFAOYSA-N caproic acid ethyl ester Natural products CCCCCC(=O)OCC SHZIWNPUGXLXDT-UHFFFAOYSA-N 0.000 claims description 5
- 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 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
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-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
- 125000002178 anthracenyl group Chemical group C1(=CC=CC2=CC3=CC=CC=C3C=C12)* 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
- 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
- 125000004663 dialkyl amino group Chemical group 0.000 claims description 4
- 125000005469 ethylenyl 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
- 150000007522 mineralic acids Chemical class 0.000 claims description 4
- 125000002524 organometallic group Chemical group 0.000 claims description 4
- 239000001294 propane Substances 0.000 claims description 4
- 229910001494 silver tetrafluoroborate Inorganic materials 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
- 125000001544 thienyl group Chemical group 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
- DVSDBMFJEQPWNO-UHFFFAOYSA-N methyllithium Chemical compound C[Li] DVSDBMFJEQPWNO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052720 vanadium Inorganic materials 0.000 claims description 3
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 claims description 3
- 229920001577 copolymer Polymers 0.000 claims description 2
- 238000010348 incorporation Methods 0.000 claims description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 2
- 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 2
- 125000003808 silyl group Chemical group [H][Si]([H])([H])[*] 0.000 claims 2
- 125000000547 substituted alkyl group Chemical group 0.000 claims 2
- 125000003107 substituted aryl group Chemical group 0.000 claims 2
- 229910052726 zirconium Inorganic materials 0.000 claims 2
- 229910017053 inorganic salt Inorganic materials 0.000 claims 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 126
- 238000006243 chemical reaction Methods 0.000 description 40
- 239000000047 product Substances 0.000 description 39
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 34
- 239000000243 solution Substances 0.000 description 34
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 28
- 238000004458 analytical method Methods 0.000 description 28
- BKIMMITUMNQMOS-UHFFFAOYSA-N nonane Chemical compound CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 description 26
- 239000012044 organic layer Substances 0.000 description 26
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 24
- 238000000769 gas chromatography-flame ionisation detection Methods 0.000 description 24
- 239000004698 Polyethylene Substances 0.000 description 15
- 229920000573 polyethylene Polymers 0.000 description 15
- 239000007791 liquid phase Substances 0.000 description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 13
- 238000001816 cooling Methods 0.000 description 13
- 238000009826 distribution Methods 0.000 description 13
- 239000007789 gas Substances 0.000 description 13
- 239000007787 solid Substances 0.000 description 13
- 239000012265 solid product Substances 0.000 description 13
- 239000000306 component Substances 0.000 description 12
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 10
- 239000002904 solvent Substances 0.000 description 7
- JLTRXTDYQLMHGR-UHFFFAOYSA-N trimethylaluminium Chemical compound C[Al](C)C JLTRXTDYQLMHGR-UHFFFAOYSA-N 0.000 description 7
- 239000007795 chemical reaction product Substances 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000004711 α-olefin Substances 0.000 description 6
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000000178 monomer Substances 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 4
- MJSNUBOCVAKFIJ-LNTINUHCSA-N chromium;(z)-4-oxoniumylidenepent-2-en-2-olate Chemical compound [Cr].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O MJSNUBOCVAKFIJ-LNTINUHCSA-N 0.000 description 4
- 239000012442 inert solvent Substances 0.000 description 4
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000006555 catalytic reaction Methods 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
- 150000004820 halides Chemical class 0.000 description 3
- 238000004128 high performance liquid chromatography Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 3
- 125000006850 spacer group Chemical group 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
- HVRUGFJYCAFAAN-UHFFFAOYSA-N 1-bromo-2-ethylbenzene Chemical compound CCC1=CC=CC=C1Br HVRUGFJYCAFAAN-UHFFFAOYSA-N 0.000 description 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-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
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- BFLUIEKBBGCQAU-UHFFFAOYSA-L [Cl-].[Cl-].C1(C=CC=C1)[Ti+2][SiH](C)C Chemical compound [Cl-].[Cl-].C1(C=CC=C1)[Ti+2][SiH](C)C BFLUIEKBBGCQAU-UHFFFAOYSA-L 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Chemical group [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- UORVGPXVDQYIDP-UHFFFAOYSA-N borane Chemical compound B UORVGPXVDQYIDP-UHFFFAOYSA-N 0.000 description 2
- 150000007942 carboxylates Chemical class 0.000 description 2
- BUSHMDIRBWMJJB-UHFFFAOYSA-N chloro-bis(2-ethylphenyl)phosphane Chemical compound CCC1=CC=CC=C1P(Cl)C1=CC=CC=C1CC BUSHMDIRBWMJJB-UHFFFAOYSA-N 0.000 description 2
- 239000012043 crude product Substances 0.000 description 2
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 2
- 125000001511 cyclopentyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C1([H])[H] 0.000 description 2
- 150000004795 grignard reagents Chemical class 0.000 description 2
- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 2
- 150000002431 hydrogen Chemical group 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- 239000003607 modifier Substances 0.000 description 2
- 150000002823 nitrates Chemical class 0.000 description 2
- 125000004433 nitrogen atom Chemical group N* 0.000 description 2
- WWZKQHOCKIZLMA-UHFFFAOYSA-M octanoate Chemical compound CCCCCCCC([O-])=O WWZKQHOCKIZLMA-UHFFFAOYSA-M 0.000 description 2
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 2
- 125000001147 pentyl group Chemical group C(CCCC)* 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- REJGOFYVRVIODZ-UHFFFAOYSA-N phosphanium;chloride Chemical class P.Cl REJGOFYVRVIODZ-UHFFFAOYSA-N 0.000 description 2
- 229920013639 polyalphaolefin Polymers 0.000 description 2
- 239000002685 polymerization catalyst Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 2
- 239000007861 trimeric product Substances 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 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
- RMSGQZDGSZOJMU-UHFFFAOYSA-N 1-butyl-2-phenylbenzene Chemical group CCCCC1=CC=CC=C1C1=CC=CC=C1 RMSGQZDGSZOJMU-UHFFFAOYSA-N 0.000 description 1
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 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
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 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 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
- 238000005481 NMR spectroscopy Methods 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000005922 Phosphane Substances 0.000 description 1
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-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
- BXLFUNWEHGJPJF-UHFFFAOYSA-M [Br-].CCC1=CC=CC=C1[Mg+] Chemical compound [Br-].CCC1=CC=CC=C1[Mg+] BXLFUNWEHGJPJF-UHFFFAOYSA-M 0.000 description 1
- 230000003213 activating effect Effects 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
- 239000012300 argon atmosphere Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- RBFQJDQYXXHULB-UHFFFAOYSA-N arsane Chemical compound [AsH3] RBFQJDQYXXHULB-UHFFFAOYSA-N 0.000 description 1
- 229910000066 arsane Inorganic materials 0.000 description 1
- 238000006664 bond formation reaction Methods 0.000 description 1
- 229910000085 borane Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 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
- 238000005553 drilling Methods 0.000 description 1
- 238000005516 engineering process Methods 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
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 1
- 238000010574 gas phase reaction Methods 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
- 239000002608 ionic liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- YSTQWZZQKCCBAY-UHFFFAOYSA-L methylaluminum(2+);dichloride Chemical compound C[Al](Cl)Cl YSTQWZZQKCCBAY-UHFFFAOYSA-L 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 229910000064 phosphane Inorganic materials 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920001296 polysiloxane Chemical group 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000002243 precursor 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 Chemical group 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- OUULRIDHGPHMNQ-UHFFFAOYSA-N stibane Chemical group [SbH3] OUULRIDHGPHMNQ-UHFFFAOYSA-N 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 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
- 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
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- 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
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- 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
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- 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 an olefin trimerisation process, a catalyst system for trimerisation of olefins and the identification and use of ligands for a catalyst system for trimerisation of olefins.
- 1-Hexene is an important commercial product. In addition to its use as a specific chemical, it is also extensively used in polymerisation processes either as a monomer or co-monomer. This invention defines a catalyst system that facilitates the production of 1-hexene from ethylene in high selectivity, while avoiding the co-production of significant quantities of other higher oligomers and polyethylene.
- a nickel catalyst comprising a chelating ligand, preferably 2-diphenyl phosphino benzoic acid (DPPBA), a nickel precursor, preferably NiCI 2 6H 2 O, and a catalyst activator, preferably sodium tetraphenylborate, catalyses the oligomerisation of ethylene to yield a mixture of linear olefins containing 1-hexene.
- DPPBA 2-diphenyl phosphino benzoic acid
- a nickel precursor 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 14-25 mass % 1- hexene (Chem Systems PERP reports 90-1 , 93-6, and 94/95S12).
- trimerisation catalysts F469
- ligands include a spacer of at least one carbon atom between the heteroatoms to allow true tridentate coordination with the chromium. Tridentate coordination complexes are generally believed to be more selective towards 1-hexene than bidentate complexes.
- An example of such a heteroatomic ligand for ethylene trimerisation is bis-(2- diethylphosphino-ethyl)-amine. Although the catalyst system containing this ligand is extremely selective towards 1-hexene (with overall 1-hexene selectivity exceeding 96 mass %), it exhibits only moderate catalyst activities.
- the ethylene trimerisation catalyst system containing (o-methoxyphenyl) 2 PN(Me)P(o-methoxyphenyl) 2 is somewhat less selective (claimed selectivities towards 1-hexene range between 75 and 91.5 mass %) than the system described in WO 03/053891 , but it is more active.
- an essential attribute of the ligands disclosed in this patent application is that at least one of the R 1 , R 2 , R 3 and R 4 groups must have a polar, or electron donating, substituent.
- This invention relates to a process for selectively producing trimeric products such as 1- hexene from olefins by using a transition metal catalyst system containing a heteroatomic ligand.
- a process for the trimerisation of olefins which process includes the step of contacting an olefinic feed stream with a catalyst system which includes a heteroatomic ligand and a transition metal compound.
- trimerisation means the catalytic reaction of a single olefinic monomer or a mixture of olefinic monomers giving products enriched in trimers derived from those olefinic monomers.
- the product stream may consist of linear and/or branched olefins
- the feedstream includes an olefin or a mixture of olefins to be trimerised and can be introduced into the process according to the invention in a continuous or batch fashion.
- the product stream includes a trimer, which trimer is produced according to the invention in a continuous or batch fashion.
- the process may include a process for trimerisation of ⁇ -olefins wherein ⁇ -olefins include 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 trimerisation of ⁇ -olefins to yield trimeric ⁇ -olefin products selectively.
- the ethylene may be contacted with the catalyst system at a pressure of 1 barg, preferably greater than 10 barg, more preferably greater than 30 barg.
- heteroatomic a ligand that contains at least two heteroatoms, which may be the same or different, and may be independently selected from any one of a group which comprises phosphorus, arsenic, antimony, sulphur, nitrogen, oxygen, bismuth and selenium.
- 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 hetero hydrocarbyl group and n and m are determined by the respective valence and oxidation state of A and C.
- the 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 phosphorus, arsenic, antimony, nitrogen and bismuth and B is a linking group between A and C.
- a and/or C may be a potential donor site for coordination with the transition metal.
- An electron donor is defined as that entity that donates electrons used in chemical, including dative covalent, bond formation.
- a and/or C may be independently oxidised by S, Se, N or O.
- a and C may be independently phosphorus or phosphorus oxidised by S or Se or N or O.
- the heteroatomic ligand may be selected from a group of ligands having at least two heteroatoms, wherein each heteroatom contains hydrocarbyl or heterohydrocarbyl groups without any electron donating substituents.
- the applicant believes that if the catalyst system contains a bidentate heteroatomic coordination complex with substituents on the ortho position of any aromatic group bound to A or C, it would lead to improvements in the selectivity of the catalyst system due to suppression of secondary trimerisation reactions.
- the applicant has surprisingly found that in most instances the presence of non-electron donating substituents is beneficial in terms of the overall reaction selectivity towards 1-hexene.
- B may be selected from any one of a group comprising: organic linking groups comprising a hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl and a substituted heterohydrocarbyl group; inorganic linking groups comprising single atom links; ionic linking groups 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, aryl, aryloxy, halogen, nitro, alkoxycarbonyl, carbonyloxy, alkoxy, aminocarbonyl, carbonylamino, dialkylamino, or derivatives thereof, and aryl substituted with any of these substituents.
- Preferred R 5 groups include alkyl groups such as methyl.
- B may exclude (CH 2 ) x Y(CH 2 ) y , where Y is -P(R 6 )-, -N(R 6 )-, -As(R 6 )-, -Sb(R 6 )- or -S- and x and y are individually 1-15 and wherein R 6 is hydrogen or a halogen or a nitro group or a hydrocarbyl or a substituted hydrocarbyl group.
- a single atom linking spacer is defined as a substituted or non-substituted atom that is bound directly to A and C.
- R 1 , R 2 , R 3 and R 4 are each independently hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl or substituted heterohydrocarbyl groups where any substituents are non-electron donating.
- the substituents may be non-polar groups.
- R 1 , R 2 , R 3 and R 4 may be substituted aromatic or substituted hetero-aromatic groups containing non-electron donating substituents on the atom adjacent to the atom bound to A or C.
- R 1 , R 2 , R 3 and R 4 may be substituted aromatic or substituted hetero-aromatic groups containing non-polar substituents on the atom adjacent to the atom bound to A or C.
- Non-polar is defined by IUPAC as an entity without a permanent electric dipole moment.
- Suitable non-polar substituents may be a methyl, ethyl, propyl, propenyl, propynyl, butyl, isopropyl, isobutyl, f-butyl, pentyl, hexyl, cyclopentyl, 2-methylcyclohexyl, cyclohexyl, cylopentadienyl, phenyl, bi-phenyl, naphthyl, tolyl, xylyl, mesityl, ethenyl, and benzyl group, or the like.
- R 1 , R 2 , R 3 and R 4 may be aromatic or hetero aromatic containing at least one non-electron donating substituent on the atom adjacent to the atom bound to A or C. More preferably R 1 , R 2 , R 3 and R 4 may be aromatic or hetero aromatic containing at least one non-polar substituent on the atom adjacent to the atom bound to A or C.
- R 1 , R 2 , R 3 and R 4 include, but are not limited to, methyl, ethyl, ethylenyl, propyl, propenyl, propynyl, butyl, cyclohexyl, 2-methylcyclohexyl, 2- ethylcyclohexyl, 2-isopropylcyclohexyl, benzyl, phenyl, tolyl, xylyl, o-methylphenyl, o- ethylphenyl, o-isopropylphenyl, o-t-butylphenyl, cumyl, mesityl, biphenyl, naphthyl, anthracenyl, methoxy, ethoxy, phenoxy, tolyloxy, dimethylamino, thiomethyl, thiophenyl, trimethylsilyl, dimethylhydrazyl and the like.
- R 1 , R 2 , R 3 and R 4 may be independently aromatic or substituted aromatic groups where the substituent on the atom adjacent to the atom bound to A or C is non-electron donating.
- R 1 , R 2 , R 3 and R 4 may be independently aromatic or substituted aromatic groups where the substituent on the atom adjacent to the atom bound to A or C is not a polar group.
- R 1 , R 2 , R 3 and R 4 may be aromatic or hetero aromatic and each of R 1 , R 2 , R 3 and R 4 should be substituted on at least one of the atoms adjacent to the atom bound to A or C by a non-electron donating group. It is also preferred that R 1 , R 2 , R 3 and R 4 be aromatic or hetero aromatic and each of R 1 , R 2 , R 3 and R 4 be substituted on at least one of the atoms adjacent to the atom bound to A or C by a non- polar group.
- 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.
- 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(o-ethylphenyl) 2 ) 2 )- benzene, 1 ,4-di-(N(P(o-ethylphenyl) 2 ) 2 )-benzene, N(CH 2 CH 2 N(P(o-ethylphenyl) 2 ) 2 ) 3 and 1 ,4-di-(P(o-ethylphenyl)N(methyl)P(o-ethylphenyl) 2 )-benzene.
- the ligands can be prepared using procedures known to one skilled in the art and procedures disclosed in published literature. Examples of these ligands are: (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 2 , (o-isopropylphenyl) 2 PN(methyl)P(o- isopropylphenyl) 2 , (o-methylphenyl) 2 PN(methyl)P(o-methylphenyl) 2 , (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl)(phenyl), (o-ethylphenyl) 2 PN(isopropyl)P(o- ethylphenyl) 2 , (o-isopropyl) 2 PN(isopropyl)P(o-isopropyl) 2 , (o-methyl) 2 PN(isopropyl)P(o- methyl) 2
- the process conditions may be selected such that the catalyst activity is more than 1 gram product per gram transition metal.
- the process may be an ⁇ -olefins trimerisation process.
- the process may be an ethylene trimerisation process.
- the process includes 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 chromium, molybdenum, tungsten, tantalum, vanadium and titanium.
- the transition metal is chromium.
- the transition metal compound which, upon mixing with the heteroatomic ligand and an activator, catalyses ethylene trimerisation in accordance with the invention may be simple inorganic or organic salts, for example halides, acetylacetonoates, carboxylates, oxides, nitrates, sulfates and the like, as well as a co-ordination or organometallic complex, for example, chromium trichloride tris-tetrahydrofuran complex, (benzene)tricarbonyl chromium, chromium hexacarbonyl, molybdenum hexacarbonyl and the like.
- the preferred transition metal compounds are chromium (III) acetylacetonoate and chromium (III) 2-ethylhexanoate.
- the heteroatomic ligand can be modified to be attached, for example, 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 another catalyst as described by D.E. Bergbreiter et al., J. Am. Chem. Soc, 1987, 109, 177-179.
- transition metal complexes can also be immobilised by binding the heteroatomic ligands to silica, silica gel, polysiloxane or alumina backbone as, for example, demonstrated 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. Some systems may be self activating. 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 hexafluoroantimonate and the like.
- Suitable organoaluminium compounds include compounds of the formula AIR 3 , where each R is independently a C r C ⁇ 2 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-/7-octylaluminium, methylaluminium dichloride, ethylaluminium dichloride, dimethylaluminium chloride, diethylaluminium chloride, aluminium isopropoxide, ethylaluminiumsesquichloride, methylaluminiumsesquichloride, and aluminoxanes.
- TMA trimethylaluminium
- TEA triethylaluminium
- TIBA tri-isobutylaluminium
- tri-/7-octylaluminium methylalum
- 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 compound 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 100 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 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 or 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 product from Grace Davison).
- reaction products may be prepared with 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 as well as aromatic hydrocarbon and halogenated hydrocarbon.
- Typical solvents include, but are not limited to, benzene, toluene, xylene, cumene, heptane, cyclohexane, 1-hexene, ionic liquids and the like.
- the process may be carried out at pressures from atmospheric to 500 barg. Ethylene pressures in the range of 10-100 barg are preferred. Particularly preferred pressures range from above 30-50 barg. Catalyst activities and/or selectivities improve with pressures above 1 barg. F469
- the process may be carried out at temperatures from -20-250 °C. Temperatures in the range of 0-120 °C are preferred. Particularly preferred temperatures range from 25- 100°C.
- 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.
- trimerisation process described herein may be used in a process in which the trimerisation of ethylene and co-polymerisation occur simultaneously leading to the incorporation of the trimerisation products into a copolymer.
- trimerisation process described in US Patent No. 5,786,431.
- the catalyst system may include a F469
- 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 hetero hydrocarbyl group and n and m is determined by the respective valence and oxidation state of A and C.
- the 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 phosphorus, arsenic, antimony, nitrogen and bismuth and B is a linking group between A and C.
- a and/or C may be a potential donor site for coordination with the transition metal.
- a and/or C may be independently oxidised by S, Se, N or O.
- a and C may be independently phosphorus or phosphorus oxidised by S or Se or N or O.
- the heteroatomic ligand may be selected from a group of ligands having at least two heteroatoms, wherein each heteroatom contains hydrocarbyl, or heterohydrocarbyl groups without any electron donating substituents.
- the applicant believes that if the catalyst system contains a bidentate heteroatomic coordination complex with substituents on the ortho position of any aromatic group bound to A or C, it would lead to improvements in the selectivity of the catalyst system due to suppression of secondary trimerisation reactions. The applicant therefore believes that in most instances the absence of such electron donating substituents is beneficial in terms of the overall reaction selectivity towards 1-hexene.
- B may be selected from any one of a group comprising: organic linking groups comprising a hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl and a substituted heterohydrocarbyl group; inorganic linking groups comprising single atom links; ionic links and a group comprising methylene, dimethylmethylene, 1,2-ethane, 1,2-phenylene, F469
- 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, aryl, aryloxy, halogen, nitro, alkoxycarbonyl, carbonyloxy, alkoxy, aminocarbonyl, carbonylamino, dialkylamino, or derivatives thereof, and aryl substituted with any of these substituents.
- Preferred R 5 groups include alkyl groups such as methyl.
- B may exclude (CH 2 ) x Y(CH 2 ) y , where Y is -P(R 6 )-, -N(R 6 )-, -As(R 6 )-, -Sb(R 6 )- or -S- and x and y are individually 1-15 and wherein R 6 is hydrogen or a halogen or a nitro group or a hydrocarbyl or a substituted hydrocarbyl group.
- a single atom linking spacer is defined as a substituted or non-substituted atom that is bound directly to A and C.
- R 1 , R 2 , R 3 and R 4 are each independently hydrocarbyl, substituted hydrocarbyl, heterohydrocarbyl or substituted heterohydrocarbyl groups where any substituents are non-electron donating.
- the substituents may be non-polar groups.
- R 1 , R 2 , R 3 and R 4 may be substituted aromatic or substituted hetero-aromatic groups containing non-electron donating substituents on the atom adjacent to the atom bound to A or C.
- R ⁇ R 2 , R 3 and R 4 may be substituted aromatic or substituted hetero-aromatic groups containing non-polar substituents on the atom adjacent to the atom bound to A or C.
- Non-polar is defined by IUPAC as an entity without a permanent electric dipole moment.
- Suitable non polar substituents may be a methyl, ethyl, propyl, propenyl, propynyl, butyl, isopropyl, isobutyl, t-butyl, pentyl, hexyl, cyclopentyl, 2-methylcyclohexyl, cyclohexyl, cylopentadienyl, phenyl, bi-phenyl, naphthyl, tolyl, xylyl, mesityl, ethenyl, and benzyl group, or the like.
- R 1 , R 2 , R 3 and R 4 may be aromatic or heteroaromatic containing at least one non-electron donating substituent on the atom adjacent to the atom bound to A or C. More preferably R 1 , R 2 , R 3 and R 4 may be aromatic or hetero aromatic containing at least one non-polar substituent on the atom adjacent to the atom bound to A or C.
- R 1 , R 2 , R 3 and R 4 include, but are not limited to, methyl, ethyl, ethylenyl, propyl, propenyl, propynyl, butyl, cyclohexyl, 2-methylcyclohexyl, 2- ethylcyclohexyl, 2-isopropylcyclohexyl, benzyl, phenyl, tolyl, xylyl, o-methylphenyl, o- ethylphenyl, o-isopropylphenyl, o-f-butylphenyl, cumyl, mesityl, biphenyl, naphthyl, anthracenyl, methoxy, ethoxy, phenoxy, tolyloxy, dimethylamino, thiomethyl, thiophenyl, trimethylsilyl, dimethylhydrazyl and the like.
- R 1 , R 2 , R 3 and R 4 may be independently aromatic or substituted aromatic groups where the substituent on the atom adjacent to the atom bound to A or C is non-electron donating.
- R 1 , R 2 , R 3 and R 4 may be independently aromatic or substituted aromatic groups where the substituent on the atom adjacent to the atom bound to A or C is not a polar group.
- R 1 , R 2 , R 3 and R 4 may be aromatic or hetero aromatic and each of R 1 , R 2 , R 3 and R 4 should be substituted on at least one of the atoms adjacent to the atom bound to A or C by a non-electron donating group. It is also preferred that R 1 , R 2 , R 3 and R 4 be aromatic or heteroaromatic and each of R 1 , R 2 , R 3 and R 4 be substituted on at least one of the atoms adjacent to the atom bound to A or C by a non- polar group.
- 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.
- the ligand may also comprise multiple (R) n A-B-C(R) m units.
- R may also comprise multiple (R) n A-B-C(R) m units.
- 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 not limiting, examples of such ligands may include 1 ,2-di-(N(P(o- F469
- the ligands can be prepared using procedures known to one skilled in the art and procedures disclosed in published literature. Specific examples of these ligands are: (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 2 , (o-isopropylphenyl) 2 PN(methyl)P(o- isopropylphenyl) 2 , (o-methylphenyl) 2 PN(methyl)P(o-methylphenyl) 2 , (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl)(phenyl), (o-ethylphenyl) 2 PN(isopropyl)P(o- ethylphenyl) 2 , (o-isopropyl) 2 PN(isopropyl)P(o-isopropyl) 2 ⁇ (o-methyl) 2 PN(isopropyl)P(o- methyl) 2, (
- the catalyst system may have a catalyst activity of more than 1 gram product per gram transition metal.
- the transition metal may be selected from chromium, molybdenum, tungsten, tantalum and titanium.
- the transition metal is chromium.
- the transition metal compound which, upon mixing with the heteroatomic ligand and an activator, catalyses ethylene trimerisation in accordance with the invention may be a simple inorganic or organic salt, for example halides, acetylacetonoates, carboxylates, oxides, nitrates, sulfates and the like, as well as a co-ordination or organometallic complex, for example, chromium trichloride tris-tetrahydrofuran complex, (benzene)tricarbonyl chromium, chromium hexacarbonyl, molybdenum hexacarbonyl and the like.
- the preferred transition metal compounds are chromium (III) acetylacetonoate and chromium (III) 2-ethylhexanoate.
- 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 methyHithium 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 compound 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 to 300:1.
- the catalyst system may also include a trialkylaluminium compound in amounts of between 0.01 to 100 mol per mol aluminoxane.
- a ligand as described above, for a catalyst system, as described above, for the trimerisation of olefins.
- the invention also extends to the identification and use of ligands suitable for use in a trimerisation of olefins process or catalyst system.
- EAO ethylaluminoxane
- the mixed heteroatomic PNP ligands were synthesised 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. et al, J. Am. Chem. Soc. 1994, 116, 22, 9869; Rajanbabu, T.V. et al, J. Org. Chem. 1997, 62, 17, 6012).
- Example 2 Ethylene trimerisation reaction using CrC fTetrahydrofuran (o- ethvIphenyl)?PN(methyl)P(o-ethylphenyl) 7 and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 45°C, while the ethylene pressure was allowed to gradually increase to 45 barg over a period of 15 minutes. 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 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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. The remainder of the organic layer was filtered to isolate the solid wax polymeric products. These solid products were dried overnight in an oven at 100°C and then weighed to yield 0.4358 g of F469
- Example 3 Ethylene trimerisation reaction using CrC Tetrahydrofuran ⁇ , (o- ethylphenyl) ? PN(methyl)P(o-ethylphenyl)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 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 trimerisation reaction using Cr(lll) acetylacetonoate, (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 2 and MAO
- Example 5 Ethylene trimerisation reaction using Cr(lll) acetylacetonoate, (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 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 10 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 trimerisation reaction using Cr(lll) acetylacetonoate, (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 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 10 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 trimerisation reaction using Cr(lll) (2-ethylhexanoate), (o- ethylphenvD PNfmethvDPfo-ethylphenyl)? and MAO
- Example 8 Ethylene trimerisation reaction using Cr(lll) (2-ethylhexanoate), (o- methylphenyl)?PN(methyl)P(o-methylphenyl) ? and MAO
- the pressure reactor was charged with ethylene after which the reactor temperature was maintained at 60°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 10 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 trimerisation reaction using Cr(lll) acetylacetonoate, (o- methylphenyl) 2 PN(Me)P(o-methylphenyl) 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 13 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 trimerisation reaction using Cr(lll) acetylacetonoate, (o- isopropylphenyl) 2 PN(methyl)P(o-isopropylphenyl) 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 13 minutes by discontinuing the F469
- Example 11 Ethylene trimerisation reaction using Cr(lll) acetylacetonoate, (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 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 30 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 trimerisation reaction using Cr(lll) acetylacetonoate, (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 2 and EAO/TMA
- 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 46 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 trimerisation reaction using Cr(octanoate) 3 , (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 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 F469
- Example 14 Ethylene trimerisation reaction using Cr(lll) acetylacetonoate, (o- ethylphenyl) 2 PN(methyl)P(o-ethylphenyl) 2 and MAO in cyclohexane as solvent
- 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 10 minutes by discontinuing the ethylene feed to the reactor and cooling the reactor to below 20°C. After releasing the excess ethylene from the autoclave, the reaction mixture 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 15 Tandem trimerisation and co-polymerisation using Cr(acacW(o- ethylphenyl) 2 -PN(methyl)P(o-ethylphenyl) 2 , cyclopentadienyl dimethylsilyl titanium dichloride and MAO
- the 300 ml Parr autoclave was charged with 60 ml anhydrous toluene as well as the previously stirred Cr(acac) 3 /(o-ethylphenyl) 2 -PN(methyl)P(o-ethylphenyl) 2 ligand solution under inert conditions.
- Approximately 600 eq methylaluminoxane (MAO) was added to the autoclave under inert conditions.
- the autoclave was connected to the HPLC pump outlet and heated to 45 °C, sealed and pressurized to 630 PSI with ethylene whilst stirring was commenced at 1200 rpm.
- the polymerization catalyst solution was added to the autoclave through the HPLC pump.
- the polymerization catalyst was added at a rate of 0.33 ml/min over a period of 60 minutes after which the reaction vessel was cooled down and quenched with ethanol.
- the autoclave was opened and the contents collected for analysis.
- the polymer collected was washed in acetone and dried in a vacuum oven for 12h at 60 °C.
- the dried polymer amounted to 12.5 g.
- Analysis of the polymer revealed two melting points at 96 °C (broad, onset at 114.92 °C) and one at 120.48 °C.
- the total amount of 1-hexene incorporated was 7 mol % ( 13 C NMR).
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Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
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BRPI0316870-0A BRPI0316870B1 (en) | 2002-12-20 | 2003-12-19 | OLEFIN TRIMERIZATION |
AU2003297544A AU2003297544A1 (en) | 2002-12-20 | 2003-12-19 | Trimerisation of olefins |
DE60331252T DE60331252D1 (en) | 2002-12-20 | 2003-12-19 | TRIMERIZATION OF OLEFINES |
CNB2003801091332A CN100540514C (en) | 2002-12-20 | 2003-12-19 | The trimerization of alkene |
US10/539,137 US7525009B2 (en) | 2002-12-20 | 2003-12-19 | Trimerisation of olefins |
CA2510190A CA2510190C (en) | 2002-12-20 | 2003-12-19 | Trimerisation of olefins |
EP03813852A EP1581341B1 (en) | 2002-12-20 | 2003-12-19 | Trimerisation of olefins |
BR0316870-0A BR0316870A (en) | 2002-12-20 | 2003-12-19 | Olefin Trimerization |
ES03813852T ES2340483T3 (en) | 2002-12-20 | 2003-12-19 | TRIMERIZATION OF OLEFINS. |
AT03813852T ATE457196T1 (en) | 2002-12-20 | 2003-12-19 | TRIMERIZATION OF OLEFINS |
JP2005511967A JP2006516265A (en) | 2002-12-20 | 2003-12-19 | Olefin trimerization |
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US43540502P | 2002-12-20 | 2002-12-20 | |
ZA2002/10339 | 2002-12-20 | ||
US60/435,405 | 2002-12-20 | ||
ZA200210339 | 2002-12-20 | ||
US47837903P | 2003-06-13 | 2003-06-13 | |
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US60/478,379 | 2003-06-13 | ||
US50930903P | 2003-10-06 | 2003-10-06 | |
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ZA200307774 | 2003-10-06 |
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PCT/ZA2003/000187 WO2004056479A1 (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/ZA2003/000186 WO2004056478A1 (en) | 2002-12-20 | 2003-12-19 | Tetramerization of olefins |
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EP (3) | EP1581341B1 (en) |
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AT (2) | ATE477053T1 (en) |
AU (3) | AU2003297546A1 (en) |
BR (6) | BR0317510A (en) |
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