WO2009050045A2 - Process for the preparation of high fluidity propylene polymers - Google Patents
Process for the preparation of high fluidity propylene polymers Download PDFInfo
- Publication number
- WO2009050045A2 WO2009050045A2 PCT/EP2008/063243 EP2008063243W WO2009050045A2 WO 2009050045 A2 WO2009050045 A2 WO 2009050045A2 EP 2008063243 W EP2008063243 W EP 2008063243W WO 2009050045 A2 WO2009050045 A2 WO 2009050045A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- propylene
- diethyl
- process according
- branched alkyl
- dineopentyl
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 35
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title claims description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 32
- 150000001875 compounds Chemical class 0.000 claims abstract description 24
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 23
- 239000011949 solid catalyst Substances 0.000 claims abstract description 15
- 150000003377 silicon compounds Chemical class 0.000 claims abstract description 10
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 9
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 8
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 6
- 239000000155 melt Substances 0.000 claims abstract description 6
- 125000005234 alkyl aluminium group Chemical group 0.000 claims abstract description 5
- 150000003890 succinate salts Chemical class 0.000 claims abstract 5
- 239000001257 hydrogen Substances 0.000 claims description 20
- 229910052739 hydrogen Inorganic materials 0.000 claims description 20
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 17
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 17
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 17
- 125000004432 carbon atom Chemical group C* 0.000 claims description 14
- 239000011777 magnesium Substances 0.000 claims description 12
- 239000010936 titanium Substances 0.000 claims description 12
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 11
- 125000004429 atom Chemical group 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 10
- 125000003710 aryl alkyl group Chemical group 0.000 claims description 9
- 125000003118 aryl group Chemical group 0.000 claims description 9
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 9
- 239000008096 xylene Substances 0.000 claims description 9
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 8
- 239000005977 Ethylene Substances 0.000 claims description 8
- 125000002877 alkyl aryl group Chemical group 0.000 claims description 8
- UVGKQRAGAYVWQV-UHFFFAOYSA-N 2,3-dimethylbutan-2-yl(trimethoxy)silane Chemical compound CO[Si](OC)(OC)C(C)(C)C(C)C UVGKQRAGAYVWQV-UHFFFAOYSA-N 0.000 claims description 7
- 125000003342 alkenyl group Chemical group 0.000 claims description 7
- 125000005842 heteroatom Chemical group 0.000 claims description 7
- 229910052710 silicon Inorganic materials 0.000 claims description 6
- 150000003609 titanium compounds Chemical class 0.000 claims description 6
- 229920001577 copolymer Polymers 0.000 claims description 5
- 125000005843 halogen group Chemical group 0.000 claims description 5
- 229920001038 ethylene copolymer Polymers 0.000 claims description 4
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 4
- 230000000379 polymerizing effect Effects 0.000 claims description 4
- 239000004711 α-olefin Substances 0.000 claims description 4
- 150000001336 alkenes Chemical class 0.000 claims description 3
- 229920001384 propylene homopolymer Polymers 0.000 claims description 3
- 238000009826 distribution Methods 0.000 abstract description 6
- 150000002367 halogens Chemical class 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 125000000008 (C1-C10) alkyl group Chemical group 0.000 abstract 1
- 238000006116 polymerization reaction Methods 0.000 description 29
- UWNADWZGEHDQAB-UHFFFAOYSA-N 2,5-dimethylhexane Chemical group CC(C)CCC(C)C UWNADWZGEHDQAB-UHFFFAOYSA-N 0.000 description 23
- 229920000642 polymer Polymers 0.000 description 20
- -1 n- butyl Chemical group 0.000 description 17
- 125000004177 diethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 12
- 239000007788 liquid Substances 0.000 description 9
- KDYFGRWQOYBRFD-UHFFFAOYSA-L succinate(2-) Chemical compound [O-]C(=O)CCC([O-])=O KDYFGRWQOYBRFD-UHFFFAOYSA-L 0.000 description 9
- 235000011147 magnesium chloride Nutrition 0.000 description 7
- 239000000178 monomer Substances 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 238000011282 treatment Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 150000002430 hydrocarbons Chemical group 0.000 description 5
- 229910010165 TiCu Inorganic materials 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 229930195733 hydrocarbon Natural products 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 150000003900 succinic acid esters Chemical class 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 3
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical group [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000002083 X-ray spectrum Methods 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 238000012662 bulk polymerization Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 125000001971 neopentyl group Chemical group [H]C([*])([H])C(C([H])([H])[H])(C([H])([H])[H])C([H])([H])[H] 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 2
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 2
- GOHPTLYPQCTZSE-UHFFFAOYSA-N 2,2-dimethylsuccinic acid Chemical compound OC(=O)C(C)(C)CC(O)=O GOHPTLYPQCTZSE-UHFFFAOYSA-N 0.000 description 1
- LVFFZQQWIZURIO-UHFFFAOYSA-N 2-phenylbutanedioic acid Chemical compound OC(=O)CC(C(O)=O)C1=CC=CC=C1 LVFFZQQWIZURIO-UHFFFAOYSA-N 0.000 description 1
- PCOCFIOYWNCGBM-UHFFFAOYSA-M 4-[(2-methylpropan-2-yl)oxy]-4-oxobutanoate Chemical compound CC(C)(C)OC(=O)CCC([O-])=O PCOCFIOYWNCGBM-UHFFFAOYSA-M 0.000 description 1
- SYQQWGGBOQFINV-FBWHQHKGSA-N 4-[2-[(2s,8s,9s,10r,13r,14s,17r)-10,13-dimethyl-17-[(2r)-6-methylheptan-2-yl]-3-oxo-1,2,6,7,8,9,11,12,14,15,16,17-dodecahydrocyclopenta[a]phenanthren-2-yl]ethoxy]-4-oxobutanoic acid Chemical compound C1CC2=CC(=O)[C@H](CCOC(=O)CCC(O)=O)C[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 SYQQWGGBOQFINV-FBWHQHKGSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 229910018540 Si C Inorganic materials 0.000 description 1
- 229910003074 TiCl4 Inorganic materials 0.000 description 1
- 239000011954 Ziegler–Natta catalyst Substances 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- IDEFBCQIICTWKE-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,2-bis(2-methylpropyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CC(C)C)(CC(C)C)CC(=O)OCC(C)(C)C IDEFBCQIICTWKE-UHFFFAOYSA-N 0.000 description 1
- ADZFLDKHGVEWSL-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-bis(2,2-dimethylpropyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CC(C)(C)C)C(CC(C)(C)C)C(=O)OCC(C)(C)C ADZFLDKHGVEWSL-UHFFFAOYSA-N 0.000 description 1
- KVVLNQWMOPCXGX-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-bis(2-ethylbutyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CC(CC)CC)C(CC(CC)CC)C(=O)OCC(C)(C)C KVVLNQWMOPCXGX-UHFFFAOYSA-N 0.000 description 1
- QUFGYPAARDNDHT-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-bis(2-methylpropyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CC(C)C)C(CC(C)C)C(=O)OCC(C)(C)C QUFGYPAARDNDHT-UHFFFAOYSA-N 0.000 description 1
- YEXQXPUBFDSHBM-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-bis(3-methylbutyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CCC(C)C)C(CCC(C)C)C(=O)OCC(C)(C)C YEXQXPUBFDSHBM-UHFFFAOYSA-N 0.000 description 1
- PTKSWGYKEGTSBF-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-bis(cyclohexylmethyl)butanedioate Chemical compound C1CCCCC1CC(C(=O)OCC(C)(C)C)C(C(=O)OCC(C)(C)C)CC1CCCCC1 PTKSWGYKEGTSBF-UHFFFAOYSA-N 0.000 description 1
- AGTSNOQZSOUYNZ-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-bis(trimethylsilyl)butanedioate Chemical compound CC(C)(C)COC(=O)C([Si](C)(C)C)C([Si](C)(C)C)C(=O)OCC(C)(C)C AGTSNOQZSOUYNZ-UHFFFAOYSA-N 0.000 description 1
- HJCDVOQEOGWEHT-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-di(propan-2-yl)butanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)C)C(C(C)C)C(=O)OCC(C)(C)C HJCDVOQEOGWEHT-UHFFFAOYSA-N 0.000 description 1
- AHIVTSBZAJNNSY-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-dibenzylbutanedioate Chemical compound C=1C=CC=CC=1CC(C(=O)OCC(C)(C)C)C(C(=O)OCC(C)(C)C)CC1=CC=CC=C1 AHIVTSBZAJNNSY-UHFFFAOYSA-N 0.000 description 1
- LLPRMYMBSZDYGM-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-diethyl-2-propan-2-ylbutanedioate Chemical compound CC(C)(C)COC(=O)C(CC)C(CC)(C(C)C)C(=O)OCC(C)(C)C LLPRMYMBSZDYGM-UHFFFAOYSA-N 0.000 description 1
- AQERQEBTYYCSSF-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2,3-ditert-butylbutanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)(C)C)C(C(C)(C)C)C(=O)OCC(C)(C)C AQERQEBTYYCSSF-UHFFFAOYSA-N 0.000 description 1
- KTGJCWXDEIGNLV-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(1,1,1-trifluoropropan-2-yl)butanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)C(F)(F)F)CC(=O)OCC(C)(C)C KTGJCWXDEIGNLV-UHFFFAOYSA-N 0.000 description 1
- NJNDDPHFDDGDQY-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(2,2-dimethylpropyl)butanedioate Chemical compound CC(C)(C)COC(=O)CC(CC(C)(C)C)C(=O)OCC(C)(C)C NJNDDPHFDDGDQY-UHFFFAOYSA-N 0.000 description 1
- KJWOIKOFBQXERA-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(2,3-dimethylbutan-2-yl)butanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)(C)C(C)C)CC(=O)OCC(C)(C)C KJWOIKOFBQXERA-UHFFFAOYSA-N 0.000 description 1
- VGEIDOBPJNLGMJ-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(2-methylpropyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CC(C)C)CC(=O)OCC(C)(C)C VGEIDOBPJNLGMJ-UHFFFAOYSA-N 0.000 description 1
- FWACQKJXPOYLQQ-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(3-methylbutyl)-2-(2-methylpropyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CC(C)C)(CCC(C)C)CC(=O)OCC(C)(C)C FWACQKJXPOYLQQ-UHFFFAOYSA-N 0.000 description 1
- AETYVAFIJAFBNZ-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(3-methylbutyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CCC(C)C)CC(=O)OCC(C)(C)C AETYVAFIJAFBNZ-UHFFFAOYSA-N 0.000 description 1
- GCKLHAHRTZPVPX-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(4-methoxyphenyl)butanedioate Chemical compound COC1=CC=C(C(CC(=O)OCC(C)(C)C)C(=O)OCC(C)(C)C)C=C1 GCKLHAHRTZPVPX-UHFFFAOYSA-N 0.000 description 1
- VSZLQEOXVFATOK-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(9h-fluoren-1-yl)butanedioate Chemical compound C12=CC=CC=C2CC2=C1C=CC=C2C(C(=O)OCC(C)(C)C)CC(=O)OCC(C)(C)C VSZLQEOXVFATOK-UHFFFAOYSA-N 0.000 description 1
- CMJRSVKGOIKARE-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-(cyclohexylmethyl)butanedioate Chemical compound CC(C)(C)COC(=O)CC(C(=O)OCC(C)(C)C)CC1CCCCC1 CMJRSVKGOIKARE-UHFFFAOYSA-N 0.000 description 1
- NOBMKPBJUKFMIM-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-benzyl-2-propan-2-ylbutanedioate Chemical compound CC(C)(C)COC(=O)CC(C(C)C)(C(=O)OCC(C)(C)C)CC1=CC=CC=C1 NOBMKPBJUKFMIM-UHFFFAOYSA-N 0.000 description 1
- HNENNRRSVVMLCB-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-benzylbutanedioate Chemical compound CC(C)(C)COC(=O)CC(C(=O)OCC(C)(C)C)CC1=CC=CC=C1 HNENNRRSVVMLCB-UHFFFAOYSA-N 0.000 description 1
- IJMIYHHICCXFMT-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-butan-2-ylbutanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)CC)CC(=O)OCC(C)(C)C IJMIYHHICCXFMT-UHFFFAOYSA-N 0.000 description 1
- UTVJXYSASDYZLE-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-butyl-2-cyclopentylbutanedioate Chemical compound CC(C)(C)COC(=O)CC(CCCC)(C(=O)OCC(C)(C)C)C1CCCC1 UTVJXYSASDYZLE-UHFFFAOYSA-N 0.000 description 1
- NNPXBUPTEQQGDP-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-cyclohexyl-2-ethylbutanedioate Chemical compound CC(C)(C)COC(=O)CC(CC)(C(=O)OCC(C)(C)C)C1CCCCC1 NNPXBUPTEQQGDP-UHFFFAOYSA-N 0.000 description 1
- HMVJOAQUCKNDSY-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-cyclohexyl-3-(3-methylbutyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CCC(C)C)C(C(=O)OCC(C)(C)C)C1CCCCC1 HMVJOAQUCKNDSY-UHFFFAOYSA-N 0.000 description 1
- WBVSZQNNFNNKNE-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-cyclohexyl-3-cyclopentylbutanedioate Chemical compound C1CCCC1C(C(=O)OCC(C)(C)C)C(C(=O)OCC(C)(C)C)C1CCCCC1 WBVSZQNNFNNKNE-UHFFFAOYSA-N 0.000 description 1
- BAZZQSBBKHVYMW-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-cyclohexyl-3-propan-2-ylbutanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)C)C(C(=O)OCC(C)(C)C)C1CCCCC1 BAZZQSBBKHVYMW-UHFFFAOYSA-N 0.000 description 1
- LKOSHICWIVXLAB-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-cyclohexylbutanedioate Chemical compound CC(C)(C)COC(=O)CC(C(=O)OCC(C)(C)C)C1CCCCC1 LKOSHICWIVXLAB-UHFFFAOYSA-N 0.000 description 1
- CFZAIAIUVWLIMV-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-cyclopropylbutanedioate Chemical compound CC(C)(C)COC(=O)CC(C(=O)OCC(C)(C)C)C1CC1 CFZAIAIUVWLIMV-UHFFFAOYSA-N 0.000 description 1
- JPILFFIEBDMDSX-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-ethyl-2-(2-methylpropyl)butanedioate Chemical compound CC(C)(C)COC(=O)C(CC(C)C)(CC)CC(=O)OCC(C)(C)C JPILFFIEBDMDSX-UHFFFAOYSA-N 0.000 description 1
- JUGAADKUCWKWDT-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-ethyl-2-methylbutanedioate Chemical compound CC(C)(C)COC(=O)C(C)(CC)CC(=O)OCC(C)(C)C JUGAADKUCWKWDT-UHFFFAOYSA-N 0.000 description 1
- GZYMFBWJQIIYIX-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-ethyl-2-tetradecylbutanedioate Chemical compound CCCCCCCCCCCCCCC(CC)(C(=O)OCC(C)(C)C)CC(=O)OCC(C)(C)C GZYMFBWJQIIYIX-UHFFFAOYSA-N 0.000 description 1
- XSPWSCMPGMVYEL-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-methoxybutanedioate Chemical compound CC(C)(C)COC(=O)C(OC)CC(=O)OCC(C)(C)C XSPWSCMPGMVYEL-UHFFFAOYSA-N 0.000 description 1
- CHKMRSWCGNKKNL-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-methyl-2,3-di(propan-2-yl)butanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)C)C(C)(C(C)C)C(=O)OCC(C)(C)C CHKMRSWCGNKKNL-UHFFFAOYSA-N 0.000 description 1
- SMMUYBXHSOZRTD-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-methyl-2-(1,1,1-trifluoropropan-2-yl)butanedioate Chemical compound CC(C)(C)COC(=O)C(C)(C(C(F)(F)F)C)CC(=O)OCC(C)(C)C SMMUYBXHSOZRTD-UHFFFAOYSA-N 0.000 description 1
- QLWSKAMMSBMSJQ-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-methyl-2-propan-2-ylbutanedioate Chemical compound CC(C)(C)COC(=O)C(C)(C(C)C)CC(=O)OCC(C)(C)C QLWSKAMMSBMSJQ-UHFFFAOYSA-N 0.000 description 1
- KMCXKSMNAJJWPC-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-propan-2-ylbutanedioate Chemical compound CC(C)(C)COC(=O)C(C(C)C)CC(=O)OCC(C)(C)C KMCXKSMNAJJWPC-UHFFFAOYSA-N 0.000 description 1
- UXXFIMLQAGKNGU-UHFFFAOYSA-N bis(2,2-dimethylpropyl) 2-trimethylsilylbutanedioate Chemical compound CC(C)(C)COC(=O)CC([Si](C)(C)C)C(=O)OCC(C)(C)C UXXFIMLQAGKNGU-UHFFFAOYSA-N 0.000 description 1
- XPNLIFFBWNEOFC-UHFFFAOYSA-N bis(2-methylpropyl) 2,2-bis(2-methylpropyl)butanedioate Chemical compound CC(C)COC(=O)CC(CC(C)C)(CC(C)C)C(=O)OCC(C)C XPNLIFFBWNEOFC-UHFFFAOYSA-N 0.000 description 1
- MPSAWYFEZAJHLR-UHFFFAOYSA-N bis(2-methylpropyl) 2,3-bis(2,2-dimethylpropyl)butanedioate Chemical compound CC(C)COC(=O)C(CC(C)(C)C)C(CC(C)(C)C)C(=O)OCC(C)C MPSAWYFEZAJHLR-UHFFFAOYSA-N 0.000 description 1
- WKNTTWKXLKQFIX-UHFFFAOYSA-N bis(2-methylpropyl) 2,3-bis(2-methylpropyl)butanedioate Chemical compound CC(C)COC(=O)C(CC(C)C)C(CC(C)C)C(=O)OCC(C)C WKNTTWKXLKQFIX-UHFFFAOYSA-N 0.000 description 1
- QHMBXAPRKPBMRN-UHFFFAOYSA-N bis(2-methylpropyl) 2,3-bis(3-methylbutyl)butanedioate Chemical compound CC(C)COC(=O)C(CCC(C)C)C(CCC(C)C)C(=O)OCC(C)C QHMBXAPRKPBMRN-UHFFFAOYSA-N 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
- SQBBHCOIQXKPHL-UHFFFAOYSA-N tributylalumane Chemical compound CCCC[Al](CCCC)CCCC SQBBHCOIQXKPHL-UHFFFAOYSA-N 0.000 description 1
- ORYGRKHDLWYTKX-UHFFFAOYSA-N trihexylalumane Chemical compound CCCCCC[Al](CCCCCC)CCCCCC ORYGRKHDLWYTKX-UHFFFAOYSA-N 0.000 description 1
- MCULRUJILOGHCJ-UHFFFAOYSA-N triisobutylaluminium Chemical compound CC(C)C[Al](CC(C)C)CC(C)C MCULRUJILOGHCJ-UHFFFAOYSA-N 0.000 description 1
- LFXVBWRMVZPLFK-UHFFFAOYSA-N trioctylalumane Chemical compound CCCCCCCC[Al](CCCCCCCC)CCCCCCCC LFXVBWRMVZPLFK-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/04—Monomers containing three or four carbon atoms
- C08F210/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/04—Monomers containing three or four carbon atoms
- C08F10/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/646—Catalysts comprising at least two different metals, in metallic form or as compounds thereof, in addition to the component covered by group C08F4/64
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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
- C08F4/65—Pretreating the metal or compound covered by group C08F4/64 before the final contacting with the metal or compound covered by group C08F4/44
- C08F4/651—Pretreating with non-metals or metal-free compounds
-
- 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
- C08F4/65—Pretreating the metal or compound covered by group C08F4/64 before the final contacting with the metal or compound covered by group C08F4/44
- C08F4/652—Pretreating with metals or metal-containing compounds
- C08F4/654—Pretreating with metals or metal-containing compounds with magnesium or compounds thereof
- C08F4/6543—Pretreating with metals or metal-containing compounds with magnesium or compounds thereof halides of magnesium
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
-
- 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
- C08F2500/00—Characteristics or properties of obtained polyolefins; Use thereof
- C08F2500/04—Broad molecular weight distribution, i.e. Mw/Mn > 6
-
- 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
- C08F2500/00—Characteristics or properties of obtained polyolefins; Use thereof
- C08F2500/12—Melt flow index or melt flow ratio
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/02—Heterophasic composition
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/16—Elastomeric ethene-propene or ethene-propene-diene copolymers, e.g. EPR and EPDM rubbers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2308/00—Chemical blending or stepwise polymerisation process with the same catalyst
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2314/00—Polymer mixtures characterised by way of preparation
- C08L2314/02—Ziegler natta catalyst
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
- C08L2666/04—Macromolecular compounds according to groups C08L7/00 - C08L49/00, or C08L55/00 - C08L57/00; Derivatives thereof
- C08L2666/06—Homopolymers or copolymers of unsaturated hydrocarbons; Derivatives thereof
Definitions
- the present invention relates to a process for the production of propylene polymers having a
- Melt Flow rate (230 0 C, 2.16 Kg) higher than 30 g/10' and preferably higher than 50 g/10' and also characterized by having broad molecular weight distribution (MWD).
- the molecular weight distribution is an important parameter for the behavior of propylene polymers.
- broadening of the molecular weight distribution brings about an improvement in terms of polymer processability (easiness of extrusion and in general flowability) and in terms of mechanical properties (higher flexural modulus).
- One of the preferred ways to obtain polymers with broad molecular weight distribution is to use catalyst systems that are intrinsically able to impart such a property to the polymer.
- WO00/63261 is representative of a document describing a Ziegler-Natta catalyst system able to provide polymers with broad MWD, which is based on (a) a catalyst component containing Mg, Ti, Cl and a succinate as internal donor, (b) an aluminum alkyl and (c) an external electron donor compound.
- Catalyst systems based on these external donors are said to provide high activity, stereoregularity and higher melting point.
- a catalyst system comprising (a) a catalyst component containing Mg, Ti, Cl and two internal electron donors having different extractability features, one selected from succinates and the other one selected from phthalates, (b) and aluminum alkyl and (c) an external electron donor compound.
- the external electron donor can be selected from monoalkyltrialkoxysilanes in order to produce polymers with a lower crystallinity.
- the low molecular weight polymers are commonly obtained by increasing the content of the chain transfer agent (molecular weight regulator).
- molecular weight regulator is hydrogen which is gaseous at the conventional polymerization conditions, its high content in the polymerization mixture increases the pressure of the reaction system making it necessary the use of equipments especially designed to withstand to higher pressure and thus more expensive.
- a possible solution, particularly for liquid-phase polymerization, would be to run that the plant at a lower temperature which can allow a reduced pressure, but this negatively impacts the efficiency of heat exchange and the relative plant productivity. Therefore, it would be necessary to have a catalyst system showing an improved hydrogen response, i.e., capability of producing polymers with a lower molecular weight in the presence of small amounts of hydrogen.
- catalysts having high hydrogen response are the Ziegler-Natta catalysts containing 1,3-diethers described for example in EP622380. Such catalysts however, are able to produce propylene polymers with high melt flow rates only in conjunction with narrow molecular weight distribution and therefore do not solve the problem.
- the solid catalyst component comprises Mg, Ti, halogen and an electron donor selected from succinates of formula (I):
- radicals Ri and R2 are a C1-C20 linear or branched alkyl, alkenyl, cycloalkyl, aryl, arylalkyl or alkylaryl group, optionally containing heteroatoms
- the radicals R3 to Re equal to or different from each other, are hydrogen or a C1-C20 linear or branched alkyl, alkenyl, cycloalkyl, aryl, arylalkyl or alkylaryl group, optionally containing heteroatoms
- the radicals R3 to Re which are joined to the same carbon atom can be linked together to form a cycle.
- Ri and R2 are preferably Ci-Cg alkyl, cycloalkyl, aryl, arylalkyl and alkylaryl groups. Particularly preferred are the compounds in which Ri and R2 are selected from primary alkyls and in particular branched primary alkyls. Examples of suitable Ri and R2 groups are methyl, ethyl, n-propyl, n- butyl, isobutyl, neopentyl, 2-ethylhexyl. Particularly preferred are ethyl, isobutyl, and neopentyl.
- R 3 to R 5 are hydrogen and R 5 is a branched alkyl, cycloalkyl, aryl, arylalkyl and alkylaryl radical having from 3 to 10 carbon atoms.
- Suitable monosubstituted succinate compounds are Diethyl sec-butylsuccinate, Diethyl thexylsuccinate, Diethyl cyclopropylsuccinate, Diethyl norbornylsuccinate, Diethyl perihydrosuccinate, Diethyl trimethylsilylsuccinate, Diethyl methoxysuccinate, Diethyl p-methoxyphenylsuccinate, Diethyl p-chlorophenylsuccinate diethyl phenylsuccinate, diethyl cyclohexylsuccinate, diethyl benzylsuccinate, diethyl cyclohexylmethylsuccinate, diethyl t-butylsuccinate, diethyl isobutylsuccinate, diethyl isopropylsuccinate, diethyl neopentylsuccinate, diethyl isopentylsuccinate
- Another preferred group of compounds within those of formula (I) is that in which at least two radicals from R 3 to R5 are different from hydrogen and are selected from C1-C20 linear or branched alkyl, alkenyl, cycloalkyl, aryl, arylalkyl or alkylaryl group, optionally containing heteroatoms. Particularly preferred are the compounds in which the two radicals different from hydrogen are linked to the same carbon atom. Furthermore, also the compounds in which at least two radicals different from hydrogen are linked to different carbon atoms, that is R 3 and R5 or R 4 and Re are particularly preferred.
- suitable disubstituted succinates are: diethyl 2-,2-dimethylsuccinate, diethyl 2-ethyl-2-methylsuccinate, diethyl 2-Benzyl-2-isopropylsuccinate, Diethyl 2-cyclohexylmethyl- 2-isobutylsuccinate, Diethyl 2-cyclopentyl-2-n-butyl succinate, Diethyl 2,2- diisobutylsuccinate, Diethyl 2-cyclohexyl-2-ethylsuccinate, Diethyl 2-isopropyl-2- methylsuccinate, Diethyl 2-tetradecyl-2 ethyl succinate, Diethyl 2-isobutyl-2-ethylsuccinate, Diethyl 2-(l-trifluoromethyl-ethyl)-2-methylsuccinate, Diethyl 2-isopentyl-2- isobutylsuccinate, Diethyl 2-phenyl
- R3 and R5 or R 4 and Re are particularly preferred.
- suitable compounds are Diethyl 2,3bis(trimethylsilyl)succinate, Diethyl 2,2- secbutyl-3-methylsuccinate, Diethyl 2-(3,3,3,trifluoropropyl)-3-methylsuccinate, Diethyl 2,3 bis(2-ethyl-butyl)succinate, Diethyl 2,3-diethyl-2-isopropylsuccinate, Diethyl 2,3- diisopropyl-2-methylsuccinate, Diethyl 2,3-dicyclohexyl-2-methyl diethyl 2,3- dibenzylsuccinate, diethyl 2,3-diisopropylsuccinate, diethyl 2,3-bis(cyclohexylmethyl)succinate, Diethyl 2,3-di-t-butyl
- the solid catalyst components in which the Ti atoms derive from a titanium compound which contains at least one Ti-halogen bond and the Mg atoms derive from magnesium chloride.
- both the titanium compound and the electron donor of formula (I) are supported on magnesium dichloride.
- at least 70% of the titanium atoms and more preferably at least 90% of them, are in the +4 valence state.
- the magnesium dichloride is in active form.
- the active form of magnesium dichloride present in the catalyst components of the invention is recognizable by the fact that in the X-ray spectrum of the catalyst component the major intensity reflection which appears in the spectrum of the non-activated magnesium dichloride (having usually surface area smaller than 3 m 2 /g) is no longer present, but in its place there is a halo with the position of the maximum intensity shifted with respect to the position of the major intensity reflection, or by the fact that the major intensity reflection presents a half-peak breadth at least 30% greater that the one of the corresponding reflection of the non-activated Mg dichloride.
- the most active forms are those in which the halo appears in the X-ray spectrum of the solid catalyst component.
- titanium compounds are the halides or the compounds of formula TiX n (OR 1 V n , where l ⁇ n ⁇ 3, X is halogen, preferably chlorine, and R 1 is Ci-Ci 0 hydrocarbon group.
- Especially preferred titanium compounds are titanium tetrachloride and the compounds of formula TiCkOR 1 where R 1 has the meaning given above and in particular selected from methyl, n-butyl or isopropyl.
- the solid catalyst component can be prepared by reacting a titanium compound of formula Ti(OR) n - y X y , where n is the valence of titanium and y is a number between 1 and n, preferably TiCU, with a magnesium chloride deriving from an adduct of formula MgCk ⁇ ROH, where p is a number between 0.1 and 6, preferably from 2 to 3.5, and R is a hydrocarbon radical having 1-18 carbon atoms.
- the adduct can be suitably prepared in spherical form by mixing alcohol and magnesium chloride in the presence of an inert hydrocarbon immiscible with the adduct, operating under stirring conditions at the melting temperature of the adduct (100-130 0 C). Then, the emulsion is quickly quenched, thereby causing the solidification of the adduct in form of spherical particles. Examples of spherical adducts prepared according to this procedure are described in US 4,399,054 and US 4,469,648.
- the so obtained adduct can be directly reacted with the Ti compound or it can be previously subjected to thermal controlled dealcoholation (80-130 0 C) so as to obtain an adduct in which the number of moles of alcohol is generally lower than 3, preferably between 0.1 and 2.5.
- the reaction with the Ti compound can be carried out by suspending the adduct (dealcoholated or as such) in cold TiCl 4 (generally 0 0 C); the mixture is heated up to 80-130 0 C and kept at this temperature for 0.5-2 hours.
- the treatment with TiCLt can be carried out one or more times.
- the internal donor can be added during the treatment with TiCL and the treatment with the electron donor compound can be repeated one or more times.
- the succinate of formula (I) is used in molar ratio with respect to the MgCL) of from 0.01 to 1 preferably from 0.05 to 0.5.
- the preparation of catalyst components in spherical form is described for example in European patent application EP-A-395083 and in the International patent application WO98/44009.
- the solid catalyst components obtained according to the above method show a surface area (by B.E.T. method) generally between 20 and 500 m 2 /g and preferably between 50 and 400 m 2 /g, and a total porosity (by B.E.T. method) higher than 0.2 cffiVg preferably between 0.2 and 0.6 cffiVg.
- the porosity (Hg method) due to pores with radius up to lO.OOOA generally ranges from 0.3 to 1.5 cffiVg, preferably from 0.45 to 1 cffiVg.
- a further method to prepare the solid catalyst component of the invention comprises halogenating magnesium dihydrocarbyloxide compounds, such as magnesium dialkoxide or diaryloxide, with solution of TiCLt in aromatic hydrocarbon (such as toluene, xylene etc.) at temperatures between 80 and 130 0 C.
- the treatment with TiCU in aromatic hydrocarbon solution can be repeated one or more times, and the succinate is added during one or more of these treatments.
- the desired succinate can be added as such or, in an alternative way, it can be obtained in situ by using an appropriate precursor capable to be transformed in the desired electron donor compound by means, for example, of known chemical reactions such as esterif ⁇ cation, transesterif ⁇ cation etc.
- the succinate of formula (I) is used in molar ratio with respect to the MgCL) of from 0.01 to 1 preferably from 0.05 to 0.5.
- the alkyl-Al compound (b) is preferably selected from the trialkyl aluminum compounds such as for example triethylaluminum, triisobutylaluminum, tri-n-butylaluminum, tri-n-hexylaluminum, tri- n-octylaluminum. It is also possible to use mixtures of trialkylaluminum's with alkylaluminum halides, alkylaluminum hydrides or alkylaluminum sesquichlorides such as AlEt 2 Cl and Al 2 Et 3 CIs.
- the silicon compound (c) is used as external electron donor and is preferably selected from the compounds in which R is a C1-C4 linear alkyl, preferably methyl or ethyl.
- R is a C1-C4 linear alkyl, preferably methyl or ethyl.
- the group R 1 is a branched alkyl which can be linked to the Si atom through a carbon atom that can be primary, secondary or tertiary.
- Non limitative examples of branched alkyls linked to the Si atom through a primary carbon atom are isobutyl, isopentyl, 2-ethylhexyl, cycloehxylmethyl.
- Non limitative examples of branched alkyls linked to the Si atom through a secondary carbon atom are isopropyl cyclopropyl, cyclopentyl, cyclohexyl.
- Non limitative examples of branched alkyls linked to the Si atom through a tertiary carbon atom are t-butyl, thexyl, (2,3-dimethyl-2-butyl), 2,3-dimethyl-2-pentyl. Silicon compounds in which the branched alkyl is linked to the Si atom through a tertiary carbon atom are preferred and, among them, thexyltrimethoxysilane is the most preferred.
- Such propylene polymers which can also be characterized by a xylene insoluble fraction at room temperature higher than 93%wt and preferably higher than 94%wt, can be used as such for a variety of applications or, most commonly, included as the crystalline component, in the heterophasic compositions which comprise, in addition to the said crystalline portion, also a fraction comprising ethylene copolymers with propylene and/or higher alpha-olef ⁇ ns usually in the range of from 10 to 90%wt containing from 20 to 80 % by weight of ethylene.
- Such ethylene copolymers have a xylene solubility at room temperature higher than 50% wt, preferably higher than 70% and more preferably higher than 80%. wt.
- the propylene polymers When included in such compositions the propylene polymers have a MFR higher than 80 g/10'and preferably higher than 100 g/10' and especially in the range 100-170 g/10' while the whole heterophasic composition can have a melt flow rate ranging from 20 to 60 g/10.
- the isotactic propylene polymers included in the heterophasic composition can reach values in the range 200-400 g/10' with a MFR range for the whole composition being from 60 to 150 g/10' and preferably from higher than lOOg/10' to 150 g/10' more preefrably from 120 to 150 g/10'.
- the heterophasic compositions so prepared are endowed with a good stiffness/impact resistance balance and excellent spiral flow characteristics.
- any kind of polymerization process can be used with the catalysts of the invention that are very versatile.
- the polymerization can be carried out for example in slurry using as diluent a liquid inert hydrocarbon, or in bulk using the liquid monomer (propylene) as a reaction medium, or in solution using either monomers or inert hydrocarbons as solvent for the nascent polymer.
- the process of the present invention is particularly advantageous for producing said isotactic propylene polymers with high fluidity in liquid phase because in such a type of process the pressure problems connected to the use of increased amounts of hydrogen is more evident.
- the liquid phase process can be either in slurry, solution or bulk (liquid monomer). This latter technology is the most preferred and can be carried out in various types of reactors such as continuous stirred tank reactors, loop reactors or plug-flow ones.
- the polymerization is generally carried out at temperature of from 20 to 120 0 C, preferably of from 40 to 85°C.
- the operating pressure is generally between 0.5 and 10 MPa, preferably between 1 and 5 MPa.
- the operating pressure is generally between 1 and 6 MPa preferably between 1.5 and 4 MPa.
- the heterophasic compositions containing a crystalline portion with high fluidity are prepared by first polymerizing in liquid monomer, preferably in loop reactor, propylene in the presence of hydrogen amounts able to give isotactic propylene polymer with a MFR higher than 50 g/10', then in a successive step ethylene and propylene or higher alpha-olefins are polymerized in a gas-phase in order to prepare the xylene soluble copolymer portion.
- the catalyst of the present invention can be used as such in the polymerization process by introducing it directly into the reactor.
- the catalyst can be pre- polymerized before being introduced into the first polymerization reactor.
- pre- polymerized means a catalyst which has been subject to a polymerization step at a low conversion degree.
- a catalyst is considered to be pre-polymerized when the amount the polymer produced is from about 0.1 up to about 1000 g per gram of solid catalyst component.
- the pre-polymerization can be carried out with the ⁇ -olef ⁇ ns selected from the same group of olefins disclosed before.
- the conversion of the pre-polymerized catalyst component is from about 0.2 g up to about 50O g per gram of solid catalyst component.
- the pre-polymerization step can be carried out at temperatures from 0 to 80 0 C preferably from 5 to 50 0 C in liquid or gas-phase.
- the pre-polymerization step can be performed in-line as a part of a continuous polymerization process or separately in a batch process.
- the batch pre-polymerization of the catalyst of the invention with ethylene in order to produce an amount of polymer ranging from 0.5 to 20 g per gram of catalyst component is particularly preferred.
- the following examples are given in order to better illustrate the invention without limiting it.
- the spiral flow evaluation comprises injecting molten polymer into the center of a hollow spiral mold, and measuring the total length of solidified resin to determine how far the material will flow before it solidifies under specified conditions of pressure and temperature:
- (A)) is produced by feeding separately in a continuous and constant flow the catalyst component in a propylene flow, the aluminum triethyl (TEAL), Thexyltrimethoxysilane as external donor, hydrogen (used as molecular weight regulator) and propylene to reach the conditions reported in table 2.
- TEAL aluminum triethyl
- Thexyltrimethoxysilane as external donor
- hydrogen used as molecular weight regulator
- the polypropylene homopolymer produced in the first reactor is discharged in a continuous flow and, after having been purged of unreacted monomers, is introduced, in a continuous flow, into the gas-phase polymerization reactor, together with quantitatively constant flow of hydrogen, ethylene and propylene in the gas state to produce a propylene/ethylene copolymer (component (B).
- component (B) Polymerization conditions, molar ratio of the reactants and composition of the copolymers obtained are shown in Table 2.
- the polymer particles exiting the final reactor are subjected to a steam treatment to remove the reactive monomers and volatile substances, and then dried.
- microspheroidal MgCl 2 -2.8C 2 H 5 OH was prepared according to the method described in ex.2 of WO98/44009 but operating on larger scale and setting the stirring conditions so as to obtain an adduct having an average particle size of 25 ⁇ m.
- Propylene homopolymer was prepared by carrying out a bulk polymerization according to the general polymerization procedure A. Specific polymerization conditions and polymer characteristics are reported in Table 1.
- Heterophasic compositions were prepared according to the general polymerization procedure B using the same catalyst system described in examples 1-3 for examples 4 and 5 while in comparison example 6 it was used the catalyst system described in example 2 of
- a Heterophasic composition was prepared according to the general polymerization procedure B using the same catalyst system described in examples 1-3 and a higher amount of hydrogen in the first step of the polymerization. Specific polymerization conditions and polymer characteristics are reported in Table 3.
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Abstract
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Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0818758A BRPI0818758B1 (en) | 2007-10-15 | 2008-10-02 | process for preparing high flow propylene polymers |
US12/734,174 US20100249330A1 (en) | 2007-10-15 | 2008-10-02 | Process for the preparation of high fluidity propylene polymers |
EP08839744.3A EP2201049B1 (en) | 2007-10-15 | 2008-10-02 | Process for the preparation of high fluidity propylene polymers |
CN200880111534.4A CN101821303B (en) | 2007-10-15 | 2008-10-02 | Process for preparation of high fluidity propylene polymers |
RU2010119499/04A RU2471811C2 (en) | 2007-10-15 | 2008-10-02 | Method of producing high-fluidity propylene polymers |
JP2010529335A JP5524068B2 (en) | 2007-10-15 | 2008-10-02 | Method for producing high flow propylene polymer |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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EP07118446 | 2007-10-15 | ||
EP07118446.9 | 2007-10-15 | ||
US99943607P | 2007-10-18 | 2007-10-18 | |
US60/999,436 | 2007-10-18 |
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EP2452956A1 (en) * | 2010-11-12 | 2012-05-16 | Borealis AG | Improved process for polymerising propylene |
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WO2019177180A1 (en) | 2018-03-16 | 2019-09-19 | Basell Poliolefine Italia S.R.L. | Polypropylene composition and molded article |
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Also Published As
Publication number | Publication date |
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BRPI0818758A2 (en) | 2015-04-07 |
BRPI0818758B1 (en) | 2018-11-21 |
CN101821303B (en) | 2013-10-30 |
RU2471811C2 (en) | 2013-01-10 |
TW200930731A (en) | 2009-07-16 |
JP5524068B2 (en) | 2014-06-18 |
US20100249330A1 (en) | 2010-09-30 |
WO2009050045A3 (en) | 2009-07-02 |
EP2201049A2 (en) | 2010-06-30 |
JP2011500907A (en) | 2011-01-06 |
RU2010119499A (en) | 2011-11-27 |
EP2201049B1 (en) | 2017-05-31 |
CN101821303A (en) | 2010-09-01 |
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