FI112664B - Förfarande för polymerisation av alfa-olefiner i gasfas - Google Patents
Förfarande för polymerisation av alfa-olefiner i gasfas Download PDFInfo
- Publication number
- FI112664B FI112664B FI931107A FI931107A FI112664B FI 112664 B FI112664 B FI 112664B FI 931107 A FI931107 A FI 931107A FI 931107 A FI931107 A FI 931107A FI 112664 B FI112664 B FI 112664B
- Authority
- FI
- Finland
- Prior art keywords
- ethylene
- catalyst
- olefins
- process according
- polymerization
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 52
- 230000008569 process Effects 0.000 title claims abstract description 43
- 239000004711 α-olefin Substances 0.000 title claims abstract description 17
- 238000006116 polymerization reaction Methods 0.000 title claims description 30
- 239000003054 catalyst Substances 0.000 claims abstract description 53
- 239000007789 gas Substances 0.000 claims abstract description 43
- 229920000642 polymer Polymers 0.000 claims abstract description 40
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000005977 Ethylene Substances 0.000 claims abstract description 37
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 150000001335 aliphatic alkanes Chemical class 0.000 claims abstract description 10
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 7
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical group CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 35
- -1 alkylaluminum compound Chemical class 0.000 claims description 19
- 239000002245 particle Substances 0.000 claims description 19
- 239000001294 propane Substances 0.000 claims description 17
- 239000011949 solid catalyst Substances 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 12
- 125000004432 carbon atom Chemical group C* 0.000 claims description 11
- 150000001336 alkenes Chemical class 0.000 claims description 9
- VXNZUUAINFGPBY-UHFFFAOYSA-N ethyl ethylene Natural products CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims description 9
- 125000000217 alkyl group Chemical group 0.000 claims description 7
- 125000003118 aryl group Chemical group 0.000 claims description 7
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 7
- 229920001577 copolymer Polymers 0.000 claims description 6
- 239000007795 chemical reaction product Substances 0.000 claims description 5
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 claims description 4
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 claims description 4
- 150000002148 esters Chemical class 0.000 claims description 4
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 claims description 4
- 150000002576 ketones Chemical class 0.000 claims description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 3
- 150000001412 amines Chemical class 0.000 claims description 2
- 238000010924 continuous production Methods 0.000 claims description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 2
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 claims 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical group CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 claims 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 claims 1
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 239000007787 solid Substances 0.000 abstract description 10
- 150000003609 titanium compounds Chemical class 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 6
- 238000012685 gas phase polymerization Methods 0.000 abstract description 6
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 abstract description 4
- 230000000379 polymerizing effect Effects 0.000 abstract description 3
- 235000011147 magnesium chloride Nutrition 0.000 abstract 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 28
- 239000012071 phase Substances 0.000 description 28
- 239000010936 titanium Substances 0.000 description 17
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 10
- 239000001257 hydrogen Substances 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 10
- 239000011777 magnesium Substances 0.000 description 9
- 229910052719 titanium Inorganic materials 0.000 description 8
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000000178 monomer Substances 0.000 description 7
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 7
- 239000011541 reaction mixture Substances 0.000 description 7
- 230000003068 static effect Effects 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000004913 activation Effects 0.000 description 5
- 239000001273 butane Substances 0.000 description 5
- 238000009826 distribution Methods 0.000 description 5
- 230000005611 electricity Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 229910052749 magnesium Inorganic materials 0.000 description 5
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 5
- 229920000573 polyethylene Polymers 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 230000001603 reducing effect Effects 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 238000005243 fluidization Methods 0.000 description 3
- 229920001903 high density polyethylene Polymers 0.000 description 3
- 230000000877 morphologic effect Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- 230000009257 reactivity Effects 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 239000012798 spherical particle Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Chemical compound CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229920001730 Moisture cure polyurethane Polymers 0.000 description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- 239000005662 Paraffin oil Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 2
- MGWAVDBGNNKXQV-UHFFFAOYSA-N diisobutyl phthalate Chemical compound CC(C)COC(=O)C1=CC=CC=C1C(=O)OCC(C)C MGWAVDBGNNKXQV-UHFFFAOYSA-N 0.000 description 2
- 238000007429 general method Methods 0.000 description 2
- 150000004820 halides Chemical class 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 150000003377 silicon compounds Chemical class 0.000 description 2
- 229920002545 silicone oil Polymers 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000012265 solid product Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 150000003623 transition metal compounds Chemical class 0.000 description 2
- OUPPKRIDJAMCCA-UHFFFAOYSA-N 1-methoxy-2-(methoxymethyl)-2,3-dimethylbutane Chemical compound COCC(C)(C(C)C)COC OUPPKRIDJAMCCA-UHFFFAOYSA-N 0.000 description 1
- BHPDSAAGSUWVMP-UHFFFAOYSA-N 3,3-bis(methoxymethyl)-2,6-dimethylheptane Chemical compound COCC(C(C)C)(COC)CCC(C)C BHPDSAAGSUWVMP-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- PMPVIKIVABFJJI-UHFFFAOYSA-N Cyclobutane Chemical compound C1CCC1 PMPVIKIVABFJJI-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 1
- 229920006450 PE-VLD Polymers 0.000 description 1
- 229910003902 SiCl 4 Inorganic materials 0.000 description 1
- 229910003910 SiCl4 Inorganic materials 0.000 description 1
- 229910003074 TiCl4 Inorganic materials 0.000 description 1
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 1
- 238000002083 X-ray spectrum Methods 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000005234 alkyl aluminium group Chemical group 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000012986 chain transfer agent Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 229910000423 chromium oxide Inorganic materials 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- SJJCABYOVIHNPZ-UHFFFAOYSA-N cyclohexyl-dimethoxy-methylsilane Chemical compound CO[Si](C)(OC)C1CCCCC1 SJJCABYOVIHNPZ-UHFFFAOYSA-N 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 1
- 229920001198 elastomeric copolymer Polymers 0.000 description 1
- 229920013728 elastomeric terpolymer Polymers 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000019256 formaldehyde Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910052735 hafnium Inorganic materials 0.000 description 1
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 230000002140 halogenating effect Effects 0.000 description 1
- 150000002367 halogens Chemical group 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Natural products C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- JQCXWCOOWVGKMT-UHFFFAOYSA-N phthalic acid diheptyl ester Natural products CCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCC JQCXWCOOWVGKMT-UHFFFAOYSA-N 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- FDNAPBUWERUEDA-UHFFFAOYSA-N silicon tetrachloride Chemical compound Cl[Si](Cl)(Cl)Cl FDNAPBUWERUEDA-UHFFFAOYSA-N 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 1
- SQBBHCOIQXKPHL-UHFFFAOYSA-N tributylalumane Chemical compound CCCC[Al](CCCC)CCCC SQBBHCOIQXKPHL-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
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 229910052726 zirconium Inorganic materials 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
- C08F2/00—Processes of polymerisation
- C08F2/34—Polymerisation in gaseous state
-
- 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
- C08F10/02—Ethene
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/901—Monomer polymerized in vapor state in presence of transition metal containing catalyst
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Polymerisation Methods In General (AREA)
Claims (16)
1. Kontinuerligt förfarande för gasfaspolymerisa-tion av eten och dess blandningar med α-olefiner CH2=CHR, 5 väri R är en alkyl-, cykloalkyl- eller arylgrupp med 1 -12 kolatomer, med användning av en katalysator som har partikeldimensioner i omradet 30 till 150 μτη, varvid kata-lysatorn är en reaktionsprodukt av (A) en Ti-förening in-nehällande minst en Ti-halogenbindning uppburen pä en ak- 10 tiv Mg-dihalogenbärare och (B) en alkylaluminiumförening, kännetecknat av att det omfattar följande steg: (a) kontakt av katalysatorkomponenterna so att eten och/eller α-olefin(er) , som har ovan definerats, är närvarande i en mängd som ligger mellan 0 och 2 0 g per 15 gram av fast katalysatorkomponent (A); (b) förpolymerisation med katalysatorn framställd säsom beskrevs under (a) av eten eller etenblandningar med en eller flera a-olefin(er), för framställning av en polymer innehällande upp tili 20 molprocent av nämnda a-ole- 20 fin (eller α-olefiner), i en mängd som ligger mellan 30 och 1 000 g per gram av fast katalysator-komponent (A) ; • ' · och : : (c) polymerisation av eten eller etenblandningar ;··; med α-olefiner CH2=CHR i gasfasen, i en eller flera reak- ·;·· 25 torer som har en fluidiserad eller mekaniskt omrörd bädd, ;v, med användning av prepolymer-katalysatorsystemet som kom- mer frän steg (b) och cirkuleririg genom reaktorerna av en alkan som har frän 3 tili 5 kolatomer, varvid den molära koncentrationen av alkanen är frän 20 tili 90 % med avse-; 30 ende pä de totala gaserna; nämda förfarande är vidare kännetecnat av att katalysatorkomponent (A) har en partikelstorlek i omrädet 30 - 150 Mm.
, 2. Förfarande enligt patentkrav 1, känneteck- ; 35 nat av att Ti-föreningen innehällar minst en Ti-halo- genbindning och minst en Ti-ORI-bindning och nämda R1 är 112664 24 en alkyl-, cykloalkyl- eller arylgrupp som har 1-12 kol-atomer eller en -COR -grupp.
3. Förfarande enligt patentkrav 1 eller 2, kän-netecknat av att i komponenten (A) f inns en intern 5 elektrondonator närvarande.
4. Förfarande enligt patentkrav 3, känneteck-nat av att en extern donatorf örering (C) f inns närvarande i katalysatorn.
5. Förfarande enligt nägot av föregäende patent- 10 krav, kännetecknat av att den mängd prepolymer som framställs i steg (b) ligger mellan 100 och 400 g/g fast katalysatorkomponent.
6. Förfarande enligt nägot av föregäende patentkrav, kännetecknat av att polymerisationen genomförs 15. tvä reaktorer, i den första av vilka frän 5 tili 60 viktprocent av den totala polymeren framställs, och väri koncentrationen av alkan är högre än i den andra reaktorn.
7. Förfarande enligt patentkrav 1 eller 2, kännetecknat av olefinen CH2=CHR är 1-buten, 1-penten, 1- 20 hexen, 4-metylpent-1-en, 1-okten.
8. Förfarande enligt patentkrav 1 eller 2, kännetecknat av att alkylaluminiumföreningen är en trial- ;,,,· kylaluminiumf örening.
9. Förfarande enligt patentkrav 3, känneteck-25 nat av att den interna elektrondonatorn väljs bland et- rar, dietrar, estrar, aminer, ketoner.
10. Förfarande enligt patentkrav 9, kännetecknat av att den interna elektrondonatorn är en ester av en aromatisk karboxylsyra. 30
11. Förfarande enligt nägot av föregäende patent krav, kännetecknat av att alkanen är propan. ,7.
12. Förfarande enligt patentkrav 1 eller 2, kän - ; netecknatav att komponenten (A) är av sfärisk form.
• 13. Polymerer och sampolymerer, känneteckna- / 35 de av att de är erhällna med förfarandena enligt nägot av patentkraven 1-12. 112664 25
14. Etenpolymerer och - sampolymerer, kanne -tecknade av att de är erhällna med förfarandena enligt nägot av patentkraven 1 - 4.
15. Etenpolymerer och -sampolymerer med sfärisk 5 form, kännetecknade av att de är erhällna med förfarandena enligt patentkrav 12.
16. Etensampolymerer, kännetecknade av att de är erhällna med förfarandena enligt patentkrav 7.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ITMI920589 | 1992-03-13 | ||
| ITMI920589A IT1254279B (it) | 1992-03-13 | 1992-03-13 | Procedimento per la polimerizzazione in fase gas delle olefine |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| FI931107A0 FI931107A0 (fi) | 1993-03-12 |
| FI931107A FI931107A (fi) | 1993-09-14 |
| FI112664B true FI112664B (sv) | 2003-12-31 |
Family
ID=11362420
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FI931107A FI112664B (sv) | 1992-03-13 | 1993-03-12 | Förfarande för polymerisation av alfa-olefiner i gasfas |
Country Status (24)
| Country | Link |
|---|---|
| US (1) | US5733987A (sv) |
| EP (1) | EP0560312B1 (sv) |
| JP (1) | JP3910219B2 (sv) |
| KR (1) | KR100268119B1 (sv) |
| CN (1) | CN1087306C (sv) |
| AT (1) | ATE182159T1 (sv) |
| AU (1) | AU658055B2 (sv) |
| BR (1) | BR9301145A (sv) |
| CA (1) | CA2087289C (sv) |
| CZ (1) | CZ288458B6 (sv) |
| DE (1) | DE69325603T2 (sv) |
| ES (1) | ES2134225T3 (sv) |
| FI (1) | FI112664B (sv) |
| GR (1) | GR3031273T3 (sv) |
| HU (1) | HU217181B (sv) |
| IL (1) | IL105024A (sv) |
| IT (1) | IT1254279B (sv) |
| MX (1) | MX9301347A (sv) |
| MY (1) | MY110349A (sv) |
| NO (1) | NO300219B1 (sv) |
| PL (1) | PL176101B1 (sv) |
| RU (1) | RU2116318C1 (sv) |
| TW (1) | TW230210B (sv) |
| ZA (1) | ZA931726B (sv) |
Families Citing this family (57)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4872047A (en) * | 1986-11-07 | 1989-10-03 | Olin Corporation | Semiconductor die attach system |
| IT1274016B (it) * | 1994-02-21 | 1997-07-14 | Spherilene Srl | Processo per la polimerizzazione in fase gas delle a-olefine |
| US5677375A (en) * | 1995-07-21 | 1997-10-14 | Union Carbide Chemicals & Plastics Technology Corporation | Process for producing an in situ polyethylene blend |
| EP1059309A3 (en) * | 1996-12-31 | 2001-09-05 | ExxonMobil Chemical Patents Inc. | Multistage method for preparing polyolefins |
| US6066701A (en) | 1996-12-31 | 2000-05-23 | Exxon Chemical Patents Inc. | Multistage method for manufacturing polyolefins |
| FI111848B (sv) | 1997-06-24 | 2003-09-30 | Borealis Tech Oy | Förfarande och anläggning för framställning av homo- och kopolymerer av propen |
| FI111846B (sv) | 1997-06-24 | 2003-09-30 | Borealis Tech Oy | Förfarande och anordning för framställning av blandningar av polypropen |
| AU5813300A (en) | 1999-06-18 | 2001-01-09 | Basell Technology Company B.V. | Catalyst components for the polymerization of olefins and catalysts therefrom obtained |
| ES2280238T3 (es) | 1999-09-10 | 2007-09-16 | Basell Poliolefine Italia S.R.L. | Catalizador para la polimerizacion de olefinas. |
| CA2398202A1 (en) * | 2000-02-08 | 2001-08-16 | Kaneka Corporation | Curable compositions |
| US6593506B1 (en) | 2000-10-12 | 2003-07-15 | Exxonmobil Chemical Patents Inc. | Olefin recovery in a polyolefin production process |
| US6495609B1 (en) | 2000-11-03 | 2002-12-17 | Exxonmobil Chemical Patents Inc. | Carbon dioxide recovery in an ethylene to ethylene oxide production process |
| JP2004522849A (ja) * | 2001-03-15 | 2004-07-29 | バセル ポリオレフィン イタリア エス．ピー．エー． | エチレンの（共）重合方法 |
| US6541578B2 (en) * | 2001-03-22 | 2003-04-01 | Nova Chemicals (International) S.A. | Increased space-time yield in gas phase polymerization |
| BR0205691A (pt) * | 2001-06-26 | 2003-07-15 | Basell Poliolefine Spa | Componentes e catalisadores para a polimerização de olefinas |
| MY136330A (en) * | 2001-12-12 | 2008-09-30 | Basell Poliolefine Spa | Process for the polymerization of olefins |
| CN1492882A (zh) * | 2001-12-24 | 2004-04-28 | ��������ϩ�����������˾ | 用于烯烃聚合的齐格勒纳塔催化剂 |
| WO2003106511A1 (en) * | 2002-06-13 | 2003-12-24 | Basell Poliolefine Italia S.P.A. | Catalyst components for the polymerization of olefins |
| CA2456951A1 (en) * | 2002-06-13 | 2003-12-24 | Basell Poliolefine Italia S.P.A. | Process for the preparation of ethylene copolymers |
| WO2004055065A1 (en) * | 2002-12-18 | 2004-07-01 | Basell Poliolefine Italia S.P.A. | Catalyst components for the polymerization of olefins |
| EP1626996B1 (en) * | 2003-05-29 | 2017-04-26 | Basell Poliolefine Italia S.r.l. | Process for the preparation of a catalyst component and components therefrom obtained |
| KR101359287B1 (ko) * | 2003-12-19 | 2014-02-10 | 바젤 폴리올레핀 게엠베하 | 에틸렌의 (공)중합 방법 |
| US20050137364A1 (en) * | 2003-12-23 | 2005-06-23 | Univation Technologies, Llc | Condensing mode operation of gas-phase polymerization reactor |
| US20050182207A1 (en) * | 2003-12-23 | 2005-08-18 | Diwaker Singh | Gas-phase process |
| CN101035816B (zh) * | 2004-10-14 | 2010-11-03 | 巴塞尔聚烯烃意大利有限责任公司 | 烯烃气相聚合的方法 |
| ES2309445T3 (es) | 2004-12-17 | 2008-12-16 | Borealis Technology Oy | Proceso para la polimerizacion de olefinas en presencia de un catalizador de polimerizacion de las mismas. |
| WO2006103171A1 (en) * | 2005-03-30 | 2006-10-05 | Basell Poliolefine Italia S.R.L. | Catalyst components for the polymerization of olefins |
| KR20070118143A (ko) * | 2005-03-30 | 2007-12-13 | 바셀 폴리올레핀 이탈리아 에스.알.엘 | 올레핀 중합용 촉매 성분 |
| BRPI0611462A2 (pt) * | 2005-03-30 | 2010-09-08 | Basell Poliolefine Srl | processo para preparar (co)polìmeros cristalinos de etileno |
| US20070060724A1 (en) * | 2005-09-13 | 2007-03-15 | Nova Chemicals Corporation And Innovene Europe Ltd. | Enhanced catalyst productivity |
| EP1926755A1 (en) * | 2005-09-19 | 2008-06-04 | Basell Poliolefine Italia S.R.L. | Gas-phase process for the polymerization of olefins |
| WO2008019802A1 (en) * | 2006-08-15 | 2008-02-21 | Basell Poliolefine Italia S.R.L. | Process for preparing catalyst components for the polymerization of olefins |
| WO2008061662A1 (en) * | 2006-11-21 | 2008-05-29 | Basell Poliolefine Italia S.R.L. | Catalyst component for the polymerization of olefins |
| EP2121773B1 (en) | 2006-12-22 | 2016-11-23 | Basell Poliolefine Italia S.r.l. | Catalyst components for the polymerization of olefins and catalysts therefrom obtained |
| CA2588352A1 (en) * | 2007-05-11 | 2008-11-11 | Nova Chemicals Corporation | Method to estimate pent values |
| CN101638448B (zh) * | 2008-08-01 | 2011-06-15 | 中国石油化工股份有限公司 | 烯烃气相连续聚合方法 |
| BRPI0917283A2 (pt) * | 2008-08-20 | 2015-11-10 | Basell Poliolefine Spa | componentes de catalisador para a polimerização de olefinas e catalisadores deles obtidos |
| KR20120031175A (ko) | 2009-06-18 | 2012-03-30 | 바셀 폴리올레핀 이탈리아 에스.알.엘 | 올레핀 중합용 촉매 성분 및 그로부터 수득된 촉매 |
| EP2330135B1 (en) | 2009-12-02 | 2012-11-07 | Borealis AG | Process for producing polyolefins |
| KR101835309B1 (ko) | 2010-08-24 | 2018-03-08 | 바셀 폴리올레핀 이탈리아 에스.알.엘 | 올레핀 중합용 촉매 성분 |
| US10138310B2 (en) | 2010-08-24 | 2018-11-27 | Equistar Chemicals, Lp | Preparation of LLDPE resins and films having low gels |
| EP2694209A1 (en) | 2011-04-01 | 2014-02-12 | Basell Poliolefine Italia S.r.l. | Catalyst components for the polymerization of olefins and catalysts therefrom obtained |
| EP2518090A1 (en) | 2011-04-28 | 2012-10-31 | Basell Poliolefine Italia S.r.l. | Catalyst components for the polymerization of olefins and catalysts therefrom obtained |
| EP2803676A1 (en) | 2013-05-16 | 2014-11-19 | Basell Polyolefine GmbH | Process for the gas-phase polymerization of ethylene or ethylene mixtures |
| CA2857456C (en) | 2014-07-22 | 2022-05-03 | Nova Chemicals Corporation | Improved control over particulate feed |
| RU2692265C2 (ru) * | 2015-03-25 | 2019-06-24 | Базелл Полиолефин Гмбх | Способы непрерывной газофазной полимеризации |
| ES2707391T3 (es) | 2015-06-23 | 2019-04-03 | Borealis Ag | Procedimiento para la producción de resinas de LLDPE |
| EP3241611B1 (en) | 2016-05-02 | 2020-03-04 | Borealis AG | A process for feeding a polymerisation catalyst |
| WO2018011156A1 (en) * | 2016-07-12 | 2018-01-18 | Total Raffinage Chimie | Catalytic process for diene dimerization |
| EP3484932A1 (en) | 2016-07-15 | 2019-05-22 | Basell Poliolefine Italia S.r.l. | Catalyst for the polymerization of olefins |
| CA3043355C (en) * | 2016-11-17 | 2020-06-30 | Basell Polyolefine Gmbh | Polyethylene composition having high swell ratio |
| KR102187011B1 (ko) | 2016-12-19 | 2020-12-07 | 바셀 폴리올레핀 이탈리아 에스.알.엘 | 올레핀의 중합용 촉매 성분 및 이로부터 얻어지는 촉매 |
| EP3483189A1 (en) | 2017-11-14 | 2019-05-15 | Borealis AG | Automated method for terminating an olefin polymerization reaction under emergency conditions |
| US12103988B2 (en) | 2018-12-18 | 2024-10-01 | Basell Polyolefine Gmbh | Gas-phase process for preparing ethylene polymers |
| CN114829413B (zh) | 2019-11-20 | 2023-04-25 | 巴塞尔聚烯烃意大利有限公司 | 制备催化剂组分的方法和由其获得的组分 |
| EP3868793A1 (en) * | 2020-02-24 | 2021-08-25 | Borealis AG | Process for producing alpha-olefin polymers in a multistage polymerization process |
| EP4251312A1 (en) | 2020-11-27 | 2023-10-04 | Borealis AG | Catalyst feed system |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3954909A (en) * | 1970-06-09 | 1976-05-04 | Naphtachimie | Method of producing solid polymers |
| JPS6020405B2 (ja) * | 1976-04-06 | 1985-05-22 | 三井東圧化学株式会社 | 低密度ポリエチレンの製造方法 |
| NL7703570A (en) * | 1977-04-01 | 1978-10-03 | Applied Photophysics Ltd | Identification system for bodies containing luminous material - uses intensity-wavelength distribution in emission spectrum for testing |
| JPS603324B2 (ja) * | 1978-12-28 | 1985-01-28 | 三井化学株式会社 | エチレン共重合体の製造方法 |
| JPS5634709A (en) * | 1979-08-31 | 1981-04-07 | Mitsui Petrochem Ind Ltd | Gas phase polymerization or copolymerization of olefin |
| JPS5767612A (en) * | 1980-10-15 | 1982-04-24 | Mitsui Petrochem Ind Ltd | Preparation of ethylene copolymer |
| FR2651234B1 (fr) * | 1989-08-29 | 1993-03-12 | Bp Chem Int Ltd | Procede de fabrication en phase gazeuse de copolymeres du propylene a l'aide d'un systeme catalytique de haute activite. |
| FR2659338B1 (fr) * | 1990-03-09 | 1993-05-07 | Bp Chemicals Snc | Procedes et dispositifs de polymerisation catalytique d'alpha-olefines en phase gazeuse. |
| IT1246614B (it) * | 1991-06-03 | 1994-11-24 | Himont Inc | Procedimento per la polimerizzazione in fase gas delle olefine |
| ES2165354T3 (es) * | 1991-07-24 | 2002-03-16 | Exxonmobil Oil Corp | Resinas de polimero de etileno mejoradas para peliculas. |
| IT1262934B (it) * | 1992-01-31 | 1996-07-22 | Montecatini Tecnologie Srl | Componenti e catalizzatori per la polimerizzazione di olefine |
| IT1262935B (it) * | 1992-01-31 | 1996-07-22 | Montecatini Tecnologie Srl | Componenti e catalizzatori per la polimerizzazione di olefine |
-
1992
- 1992-03-13 IT ITMI920589A patent/IT1254279B/it active IP Right Grant
-
1993
- 1993-03-09 MY MYPI93000419A patent/MY110349A/en unknown
- 1993-03-10 ES ES93103809T patent/ES2134225T3/es not_active Expired - Lifetime
- 1993-03-10 EP EP93103809A patent/EP0560312B1/en not_active Expired - Lifetime
- 1993-03-10 DE DE69325603T patent/DE69325603T2/de not_active Expired - Fee Related
- 1993-03-10 AT AT93103809T patent/ATE182159T1/de not_active IP Right Cessation
- 1993-03-10 ZA ZA931726A patent/ZA931726B/xx unknown
- 1993-03-11 CZ CZ1993403A patent/CZ288458B6/cs not_active IP Right Cessation
- 1993-03-11 IL IL10502493A patent/IL105024A/en not_active IP Right Cessation
- 1993-03-11 MX MX9301347A patent/MX9301347A/es not_active IP Right Cessation
- 1993-03-11 BR BR9301145A patent/BR9301145A/pt not_active IP Right Cessation
- 1993-03-12 JP JP05220993A patent/JP3910219B2/ja not_active Expired - Fee Related
- 1993-03-12 US US08/030,654 patent/US5733987A/en not_active Expired - Fee Related
- 1993-03-12 RU RU93004614/04A patent/RU2116318C1/ru active
- 1993-03-12 AU AU35189/93A patent/AU658055B2/en not_active Ceased
- 1993-03-12 HU HU9300717A patent/HU217181B/hu not_active IP Right Cessation
- 1993-03-12 NO NO930910A patent/NO300219B1/no not_active IP Right Cessation
- 1993-03-12 PL PL93298042A patent/PL176101B1/pl unknown
- 1993-03-12 FI FI931107A patent/FI112664B/sv active
- 1993-03-13 KR KR1019930003837A patent/KR100268119B1/ko not_active IP Right Cessation
- 1993-03-13 CN CN93104325A patent/CN1087306C/zh not_active Expired - Fee Related
- 1993-03-15 CA CA002087289A patent/CA2087289C/en not_active Expired - Fee Related
- 1993-04-23 TW TW082103150A patent/TW230210B/zh active
-
1999
- 1999-09-22 GR GR990402371T patent/GR3031273T3/el unknown
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| GB | Transfer or assigment of application |
Owner name: MONTELL TECHNOLOGY COMPANY BV |