KR20020038813A - 폴리이소부텐의 연속 제조 방법 - Google Patents
폴리이소부텐의 연속 제조 방법 Download PDFInfo
- Publication number
- KR20020038813A KR20020038813A KR1020027004590A KR20027004590A KR20020038813A KR 20020038813 A KR20020038813 A KR 20020038813A KR 1020027004590 A KR1020027004590 A KR 1020027004590A KR 20027004590 A KR20027004590 A KR 20027004590A KR 20020038813 A KR20020038813 A KR 20020038813A
- Authority
- KR
- South Korea
- Prior art keywords
- polymerization
- isobutene
- polyisobutene
- boron trifluoride
- concentration
- Prior art date
Links
- 229920002367 Polyisobutene Polymers 0.000 title claims abstract description 62
- 238000000034 method Methods 0.000 title claims abstract description 52
- 238000010924 continuous production Methods 0.000 title claims abstract description 5
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 claims abstract description 129
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 claims abstract description 71
- 238000006243 chemical reaction Methods 0.000 claims abstract description 60
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 39
- 229910015900 BF3 Inorganic materials 0.000 claims abstract description 35
- 239000007788 liquid Substances 0.000 claims abstract description 32
- 230000008569 process Effects 0.000 claims abstract description 32
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 29
- 150000001875 compounds Chemical class 0.000 claims abstract description 29
- 239000001301 oxygen Substances 0.000 claims abstract description 29
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 29
- 239000012071 phase Substances 0.000 claims abstract description 29
- 239000003054 catalyst Substances 0.000 claims abstract description 23
- 239000007791 liquid phase Substances 0.000 claims abstract description 11
- 125000004432 carbon atom Chemical group C* 0.000 claims description 9
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 8
- 150000003333 secondary alcohols Chemical class 0.000 claims description 7
- 230000000379 polymerizing effect Effects 0.000 claims description 4
- 239000012429 reaction media Substances 0.000 claims description 2
- 125000004122 cyclic group Chemical group 0.000 claims 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 35
- 239000002904 solvent Substances 0.000 description 20
- 239000000203 mixture Substances 0.000 description 11
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000002360 preparation method Methods 0.000 description 8
- 239000011541 reaction mixture Substances 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 7
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 238000009826 distribution Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 150000001983 dialkylethers Chemical class 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 150000001336 alkenes Chemical class 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 3
- 125000002573 ethenylidene group Chemical group [*]=C=C([H])[H] 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 3
- 239000002685 polymerization catalyst Substances 0.000 description 3
- 239000000376 reactant Substances 0.000 description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 3
- 238000002798 spectrophotometry method Methods 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 238000001644 13C nuclear magnetic resonance spectroscopy Methods 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 150000001735 carboxylic acids Chemical class 0.000 description 2
- 238000010538 cationic polymerization reaction Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 229960001701 chloroform Drugs 0.000 description 2
- IAQRGUVFOMOMEM-ARJAWSKDSA-N cis-but-2-ene Chemical compound C\C=C/C IAQRGUVFOMOMEM-ARJAWSKDSA-N 0.000 description 2
- 238000006356 dehydrogenation reaction Methods 0.000 description 2
- JVSWJIKNEAIKJW-UHFFFAOYSA-N dimethyl-hexane Natural products CCCCCC(C)C JVSWJIKNEAIKJW-UHFFFAOYSA-N 0.000 description 2
- 238000007306 functionalization reaction Methods 0.000 description 2
- 238000005227 gel permeation chromatography Methods 0.000 description 2
- 229940052308 general anesthetics halogenated hydrocarbons Drugs 0.000 description 2
- 150000008282 halocarbons 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
- 238000011065 in-situ storage Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000001282 iso-butane Substances 0.000 description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- -1 secondary-butyl Chemical group 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000011877 solvent mixture Substances 0.000 description 2
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- RBACIKXCRWGCBB-UHFFFAOYSA-N 1,2-Epoxybutane Chemical compound CCC1CO1 RBACIKXCRWGCBB-UHFFFAOYSA-N 0.000 description 1
- HHBZZTKMMLDNDN-UHFFFAOYSA-N 2-butan-2-yloxybutane Chemical compound CCC(C)OC(C)CC HHBZZTKMMLDNDN-UHFFFAOYSA-N 0.000 description 1
- QHJLNXCHSKDYHR-UHFFFAOYSA-N 2-propan-2-yloxybutane Chemical compound CCC(C)OC(C)C QHJLNXCHSKDYHR-UHFFFAOYSA-N 0.000 description 1
- USQOVYLRWBOSQC-HNNXBMFYSA-N CCCCCCNC(=O)Oc1cccc(c1)-c1ccc(cc1F)[C@H](C)C(O)=O Chemical compound CCCCCCNC(=O)Oc1cccc(c1)-c1ccc(cc1F)[C@H](C)C(O)=O USQOVYLRWBOSQC-HNNXBMFYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- PMPVIKIVABFJJI-UHFFFAOYSA-N Cyclobutane Chemical compound C1CCC1 PMPVIKIVABFJJI-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 238000004566 IR spectroscopy Methods 0.000 description 1
- 238000004497 NIR spectroscopy Methods 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 1
- 125000005234 alkyl aluminium group Chemical group 0.000 description 1
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 1
- 150000001414 amino alcohols Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000009918 complex formation Effects 0.000 description 1
- 230000000536 complexating effect Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000006735 epoxidation reaction Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 150000002374 hemiaminals Chemical class 0.000 description 1
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 description 1
- 125000003187 heptyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000007037 hydroformylation reaction Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 125000002347 octyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 125000001147 pentyl group Chemical group C(CCCC)* 0.000 description 1
- 238000005375 photometry Methods 0.000 description 1
- 229920001281 polyalkylene Polymers 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 150000003138 primary alcohols Chemical class 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000012264 purified product Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000012925 reference material Substances 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 125000002914 sec-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 238000004230 steam cracking Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 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
- 238000011144 upstream manufacturing Methods 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
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/08—Butenes
- C08F110/10—Isobutene
-
- 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
- C08F2/001—Multistage polymerisation processes characterised by a change in reactor conditions without deactivating the intermediate polymer
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Polymerization Catalysts (AREA)
- Polymerisation Methods In General (AREA)
Abstract
Description
Claims (10)
- 수평균 분자량 MN이 500 내지 50,000 이고, 말단 이중 결합 함량이 50 몰% 이상인 폴리이소부텐의 연속 제조 방법으로서,상기 방법은 +40℃ 이하의 온도 및 삼불화붕소 및 하나 이상의 산소 함유 화합물을 포함하는 촉매가 존재하는 액상 내에서 이소부텐을 단단 또는 다단으로 연속 중합하는 단계를 포함하며,적어도 제1 중합 단계에서 상기 액체 반응상의 점도가 6 내지 20 mm2/s(DIN 51562에 따라 측정함)인 방법.
- 제1항에 있어서, 상기 중합은 정상 상태 이소부텐 농도인 1 내지 20 중량%에서 수행되는 방법.
- 제1항 또는 제2항에 있어서, 상기 중합은 일정한 점도에서 수행되는 방법.
- 제1항 내지 제3항중 어느 한 항에 있어서, 삼불화붕소로 계산한 상기 액체상내 촉매 농도가 0.01 내지 1 중량%인 방법.
- 제1항 내지 제4항중 어느 한 항에 있어서, 삼불화붕소 대 산소 함유 화합물의 몰비가 1:1 내지 1:2인 방법.
- 제1항 내지 제5항중 어느 한 항에 있어서, 상기 산소 함유 화합물이 3 내지 20개의 탄소원자로 이루어지는 1종 이상의 2차 알콜 A를 포함하는 것인 방법.
- 제6항에 있어서, 상기 산소 함유 화합물이 일반식 R1-O-R2(식중, R1및 R2는 서로 개별적으로 1 내지 10개의 탄소 원자로 이루어지는 일차 또는 이차 알킬 라디칼임)인 1종 이상의 디알킬 에테르 B를 추가로 포함하는 것인 방법.
- 제1항 내지 제7항중 어느 한 항에 있어서, 상기 중합이 단단 중합인 방법.
- 제1항 내지 제8항중 어느 한 항에 있어서, 상기 중합이 공급/순환 비가 1:5 내지 1:500 인 순환 방식으로 수행되는 방법.
- 제1항 내지 제9항중 어느 한 항에 있어서, 액체 반응상의 온도 TR, 액체 반응상의 점도 ηR및 액체 반응상의 이소부텐 농도 CI로 구성되는 군으로부터 선택되는 반응 매개변수중 하나 이상의 반응 매개 변수가 산소 함유 화합물의 첨가에 의해 조절되는 방법.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19948947A DE19948947A1 (de) | 1999-10-11 | 1999-10-11 | Verfahren zur kontinuierlichen Herstellung von Polyisobutenen |
DE19948947.5 | 1999-10-11 |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20020038813A true KR20020038813A (ko) | 2002-05-23 |
KR100714152B1 KR100714152B1 (ko) | 2007-05-07 |
Family
ID=7925238
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020027004590A KR100714152B1 (ko) | 1999-10-11 | 2000-10-10 | 폴리이소부텐의 연속 제조 방법 |
Country Status (14)
Country | Link |
---|---|
US (1) | US6642329B1 (ko) |
EP (1) | EP1240216B1 (ko) |
JP (1) | JP5166663B2 (ko) |
KR (1) | KR100714152B1 (ko) |
CN (1) | CN1142198C (ko) |
AT (1) | ATE263786T1 (ko) |
AU (1) | AU1271501A (ko) |
CA (1) | CA2386302A1 (ko) |
DE (2) | DE19948947A1 (ko) |
ES (1) | ES2219411T3 (ko) |
HU (1) | HUP0203150A3 (ko) |
MX (1) | MXPA02003472A (ko) |
MY (1) | MY123142A (ko) |
WO (1) | WO2001027172A1 (ko) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20140112542A (ko) * | 2012-01-09 | 2014-09-23 | 바스프 에스이 | 폴리아이소부틸렌의 연속 제조 방법 |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6884858B2 (en) * | 1999-10-19 | 2005-04-26 | Texas Petrochemicals Lp | Process for preparing polyolefin products |
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DE10118181A1 (de) | 2001-04-11 | 2002-10-17 | Basf Ag | Abtrennung nicht umgesetzten Isobutens bei der Polymerisation von Isobuten |
AU2002257288A1 (en) * | 2001-06-08 | 2002-12-23 | Texas Petrochemicals Lp | Improved cling film with enhanced polyisobutylene tackifier |
DE10142285A1 (de) * | 2001-08-29 | 2003-03-20 | Basf Ag | Polymerzusammensetzung, enthaltend wenigstens ein mittelmolekulares reaktives Polyisobuten |
DE102005031527A1 (de) * | 2005-06-30 | 2007-01-04 | Gardena Manufacturing Gmbh | Aufbewahrungseinrichtung für Gartenschlauch |
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CN101732976B (zh) * | 2009-12-31 | 2012-06-20 | 中电投远达环保工程有限公司 | 改善烟气脱硫工艺中脱硫石膏品质的方法及烟气脱硫装置 |
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JP6126612B2 (ja) * | 2011-10-26 | 2017-05-10 | ティーピーシー・グループ・エルエルシー | 高い速度と循環量で調製されたポリイソブチレン |
US11072570B2 (en) | 2012-01-09 | 2021-07-27 | Basf Se | Process for continuously preparing polyisobutylene |
CN104203997B (zh) | 2012-02-17 | 2016-08-17 | 巴斯夫欧洲公司 | 三氟化硼催化剂复合物以及制备高反应性异丁烯均聚物的方法 |
US8853336B2 (en) | 2012-02-17 | 2014-10-07 | Basf Se | Boron trifluoride-catalyst complex and process for preparing high-reactivity isobutene homopolymers |
CN103788317B (zh) * | 2012-10-30 | 2016-05-25 | 中国石油化工股份有限公司 | 一种含烯烃类不饱和键的聚合物加氢反应方法 |
WO2019011814A1 (en) * | 2017-07-13 | 2019-01-17 | Arlanxeo Deutschland Gmbh | PROCESS FOR THE PRODUCTION OF ISOBUTENE POLYMERS WITH ENHANCED TEMPERATURE CONTROL |
JP6883500B2 (ja) * | 2017-09-27 | 2021-06-09 | 株式会社カネカ | 重合体の製造方法 |
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EP3970848A4 (en) * | 2019-05-16 | 2023-01-25 | Nisso Engineering Co., Ltd. | CHEMICAL REACTION SYSTEM AND DEVICE SUITABLE FOR LOW-FLOW REACTIONS |
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DE2702604C2 (de) | 1977-01-22 | 1984-08-30 | Basf Ag, 6700 Ludwigshafen | Polyisobutene |
GB8329082D0 (en) | 1983-11-01 | 1983-12-07 | Bp Chem Int Ltd | Low molecular weight polymers of 1-olefins |
BE1006694A5 (fr) * | 1991-06-22 | 1994-11-22 | Basf Ag | Procede de preparation de polyisobutenes extremement reactifs. |
DE19520078A1 (de) * | 1995-06-07 | 1996-12-12 | Basf Ag | Verfahren zur Herstellung von niedermolekularem, hochreaktivem Polyisobuten |
DE19619267A1 (de) * | 1996-05-13 | 1997-11-20 | Basf Ag | Verfahren zur Herstellung von mittelmolekularem, hochreaktivem Polyisobuten |
DE19645430A1 (de) | 1996-11-04 | 1998-05-07 | Basf Ag | Polyolefine und deren funktionalisierte Derivate |
JP3795666B2 (ja) * | 1997-03-07 | 2006-07-12 | 新日本石油化学株式会社 | ブテンポリマーの製造方法 |
GB9707075D0 (en) * | 1997-04-08 | 1997-05-28 | Bp Chem Int Ltd | Polymerisation process |
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1999
- 1999-10-11 DE DE19948947A patent/DE19948947A1/de not_active Withdrawn
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2000
- 2000-10-04 MY MYPI20004640A patent/MY123142A/en unknown
- 2000-10-10 EP EP00974382A patent/EP1240216B1/de not_active Expired - Lifetime
- 2000-10-10 CN CNB008141134A patent/CN1142198C/zh not_active Expired - Lifetime
- 2000-10-10 US US10/089,724 patent/US6642329B1/en not_active Expired - Lifetime
- 2000-10-10 AT AT00974382T patent/ATE263786T1/de not_active IP Right Cessation
- 2000-10-10 CA CA002386302A patent/CA2386302A1/en not_active Abandoned
- 2000-10-10 JP JP2001530388A patent/JP5166663B2/ja not_active Expired - Lifetime
- 2000-10-10 DE DE50006019T patent/DE50006019D1/de not_active Expired - Lifetime
- 2000-10-10 ES ES00974382T patent/ES2219411T3/es not_active Expired - Lifetime
- 2000-10-10 KR KR1020027004590A patent/KR100714152B1/ko active IP Right Grant
- 2000-10-10 HU HU0203150A patent/HUP0203150A3/hu unknown
- 2000-10-10 WO PCT/EP2000/009972 patent/WO2001027172A1/de active IP Right Grant
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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KR20140112542A (ko) * | 2012-01-09 | 2014-09-23 | 바스프 에스이 | 폴리아이소부틸렌의 연속 제조 방법 |
Also Published As
Publication number | Publication date |
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DE50006019D1 (de) | 2004-05-13 |
ES2219411T3 (es) | 2004-12-01 |
MY123142A (en) | 2006-05-31 |
HUP0203150A3 (en) | 2004-06-28 |
JP2003511526A (ja) | 2003-03-25 |
EP1240216B1 (de) | 2004-04-07 |
ATE263786T1 (de) | 2004-04-15 |
EP1240216A1 (de) | 2002-09-18 |
CA2386302A1 (en) | 2001-04-19 |
JP5166663B2 (ja) | 2013-03-21 |
CN1142198C (zh) | 2004-03-17 |
HUP0203150A2 (hu) | 2002-12-28 |
US6642329B1 (en) | 2003-11-04 |
AU1271501A (en) | 2001-04-23 |
WO2001027172A1 (de) | 2001-04-19 |
CN1378566A (zh) | 2002-11-06 |
KR100714152B1 (ko) | 2007-05-07 |
MXPA02003472A (es) | 2002-08-20 |
DE19948947A1 (de) | 2001-04-12 |
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