CN104592425B - A kind of cycloheptatriene base rare-earth metal catalyst, preparation method and application - Google Patents
A kind of cycloheptatriene base rare-earth metal catalyst, preparation method and application Download PDFInfo
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- CN104592425B CN104592425B CN201510059201.3A CN201510059201A CN104592425B CN 104592425 B CN104592425 B CN 104592425B CN 201510059201 A CN201510059201 A CN 201510059201A CN 104592425 B CN104592425 B CN 104592425B
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- CN
- China
- Prior art keywords
- cycloheptatrienyl
- rare earth
- earth metal
- hydride
- aluminum
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000003054 catalyst Substances 0.000 title claims abstract description 86
- 229910052761 rare earth metal Inorganic materials 0.000 title claims abstract description 52
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- CHVJITGCYZJHLR-UHFFFAOYSA-N cyclohepta-1,3,5-triene Chemical compound C1C=CC=CC=C1 CHVJITGCYZJHLR-UHFFFAOYSA-N 0.000 title claims description 9
- 150000002910 rare earth metals Chemical class 0.000 title claims description 8
- -1 cycloheptatrienyl rare earth metal Chemical class 0.000 claims abstract description 109
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims abstract description 53
- 239000003446 ligand Substances 0.000 claims abstract description 38
- 238000003756 stirring Methods 0.000 claims abstract description 28
- 125000002188 cycloheptatrienyl group Chemical group C1(=CC=CC=CC1)* 0.000 claims abstract description 23
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims abstract description 21
- 150000001336 alkenes Chemical class 0.000 claims abstract description 19
- 239000000178 monomer Substances 0.000 claims abstract description 19
- 150000001345 alkine derivatives Chemical class 0.000 claims abstract description 17
- MDYOLVRUBBJPFM-UHFFFAOYSA-N tropolone Chemical compound OC1=CC=CC=CC1=O MDYOLVRUBBJPFM-UHFFFAOYSA-N 0.000 claims abstract description 16
- YYROPELSRYBVMQ-UHFFFAOYSA-N 4-toluenesulfonyl chloride Chemical compound CC1=CC=C(S(Cl)(=O)=O)C=C1 YYROPELSRYBVMQ-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000007334 copolymerization reaction Methods 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 8
- 238000004440 column chromatography Methods 0.000 claims abstract description 6
- 238000001953 recrystallisation Methods 0.000 claims abstract description 4
- 238000006243 chemical reaction Methods 0.000 claims description 71
- 239000000243 solution Substances 0.000 claims description 33
- 239000000203 mixture Substances 0.000 claims description 31
- 239000000047 product Substances 0.000 claims description 28
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 27
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 26
- 239000002904 solvent Substances 0.000 claims description 22
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 19
- 125000005234 alkyl aluminium group Chemical group 0.000 claims description 18
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 claims description 14
- 239000000126 substance Substances 0.000 claims description 13
- 239000003153 chemical reaction reagent Substances 0.000 claims description 12
- 239000000376 reactant Substances 0.000 claims description 12
- 150000003839 salts Chemical class 0.000 claims description 11
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 10
- 229910052782 aluminium Inorganic materials 0.000 claims description 10
- 150000001875 compounds Chemical class 0.000 claims description 9
- 239000012043 crude product Substances 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 239000012074 organic phase Substances 0.000 claims description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- 150000001412 amines Chemical class 0.000 claims description 7
- JFNLZVQOOSMTJK-KNVOCYPGSA-N norbornene Chemical compound C1[C@@H]2CC[C@H]1C=C2 JFNLZVQOOSMTJK-KNVOCYPGSA-N 0.000 claims description 7
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical compound O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 claims description 7
- UEXCJVNBTNXOEH-UHFFFAOYSA-N Ethynylbenzene Chemical group C#CC1=CC=CC=C1 UEXCJVNBTNXOEH-UHFFFAOYSA-N 0.000 claims description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 6
- 125000003545 alkoxy group Chemical group 0.000 claims description 6
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 claims description 6
- 150000001925 cycloalkenes Chemical class 0.000 claims description 6
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- 125000001424 substituent group Chemical group 0.000 claims description 6
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 claims description 6
- 125000001544 thienyl group Chemical group 0.000 claims description 6
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- 150000001638 boron Chemical class 0.000 claims description 5
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 5
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 5
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims description 4
- ZGEGCLOFRBLKSE-UHFFFAOYSA-N 1-Heptene Chemical compound CCCCCC=C ZGEGCLOFRBLKSE-UHFFFAOYSA-N 0.000 claims description 4
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 claims description 4
- CRSBERNSMYQZNG-UHFFFAOYSA-N 1-dodecene Chemical compound CCCCCCCCCCC=C CRSBERNSMYQZNG-UHFFFAOYSA-N 0.000 claims description 4
- GQEZCXVZFLOKMC-UHFFFAOYSA-N 1-hexadecene Chemical compound CCCCCCCCCCCCCCC=C GQEZCXVZFLOKMC-UHFFFAOYSA-N 0.000 claims description 4
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 claims description 4
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- HFDVRLIODXPAHB-UHFFFAOYSA-N 1-tetradecene Chemical compound CCCCCCCCCCCCC=C HFDVRLIODXPAHB-UHFFFAOYSA-N 0.000 claims description 4
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- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical group [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 4
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000002947 alkylene group Chemical group 0.000 claims description 4
- 125000003277 amino group Chemical group 0.000 claims description 4
- 239000008346 aqueous phase Substances 0.000 claims description 4
- LKRBKNPREDAJJQ-UHFFFAOYSA-M chloro-di(propan-2-yl)alumane Chemical compound [Cl-].CC(C)[Al+]C(C)C LKRBKNPREDAJJQ-UHFFFAOYSA-M 0.000 claims description 4
- MGNZXYYWBUKAII-UHFFFAOYSA-N cyclohexa-1,3-diene Chemical compound C1CC=CC=C1 MGNZXYYWBUKAII-UHFFFAOYSA-N 0.000 claims description 4
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 4
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- 150000002825 nitriles Chemical class 0.000 claims description 4
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 4
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 claims description 4
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 4
- ZIYNWDQDHKSRCE-UHFFFAOYSA-N tricyclohexylalumane Chemical compound C1CCCCC1[Al](C1CCCCC1)C1CCCCC1 ZIYNWDQDHKSRCE-UHFFFAOYSA-N 0.000 claims description 4
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- 230000003197 catalytic effect Effects 0.000 claims description 3
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Landscapes
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
本发明公开了一种环庚三烯基稀土金属催化剂、制备方法及应用,属于催化剂领域。所述方法步骤如下:首先,将环庚三烯酚酮、对甲苯磺酰氯和三乙胺加入到反应器中,在氮气氛围下反应一段时间,再将胺基取代物加入其中,过夜反应,重结晶得纯产物后,和Et3OBF4的溶液反应几小时后,再滴加胺基取代物,搅拌过夜,柱层析纯化得环庚三烯基配体;其次,将配体滴加到溶有LnR3的甲苯溶液中,室温下搅拌反应一段时间后过滤,浓缩,重结晶后得环庚三烯基稀土金属催化剂。所述催化剂原料易得,可应用到多种单体的聚合反应,包括烯烃、炔烃、极性单体的均聚及共聚合反应,或分别与CO2的共聚反应;所述催化剂制备方法简单,经济环保,应用范围广,适合工业化生产。
The invention discloses a cycloheptatrienyl rare earth metal catalyst, a preparation method and an application, and belongs to the field of catalysts. The steps of the method are as follows: first, add tropolone, p-toluenesulfonyl chloride and triethylamine into the reactor, react for a period of time under a nitrogen atmosphere, then add amino substituents therein, and react overnight, After recrystallization to obtain the pure product, after reacting with the solution of Et 3 OBF 4 for several hours, add the amino substituent dropwise, stir overnight, and purify by column chromatography to obtain the cycloheptatrienyl ligand; secondly, add the ligand dropwise into a toluene solution in which LnR3 is dissolved, stirred at room temperature for a period of time, filtered, concentrated, and recrystallized to obtain a cycloheptatrienyl rare earth metal catalyst. The catalyst raw material is easy to get, and can be applied to the polymerization of various monomers, including the homopolymerization and copolymerization of olefins, alkynes, and polar monomers, or the copolymerization with CO respectively; the preparation method of the catalyst The method is simple, economical and environment-friendly, has a wide range of applications and is suitable for industrialized production.
Description
技术领域technical field
本发明涉及一种环庚三烯基稀土金属催化剂、制备方法及应用,属于催化剂技术领域。The invention relates to a cycloheptatrienyl rare earth metal catalyst, a preparation method and an application, and belongs to the technical field of catalysts.
背景技术Background technique
共轭效应指在共轭体系中由于原子间的相互影响而使体系内的π电子(或p电子)分布发生变化的一种电子效应,是有机化学中一种重要的电子效应。它能使分子中电子云密度的分布发生改变(共平面化),内能减少,键长趋于平均化,折射率升高,整个分子更趋稳定。对于这些分子的结构及其性质的研究,在理论上和实用上都具有非常重要的意义,因此这类化合物引起了人们的广泛兴趣。The conjugation effect refers to an electronic effect that changes the distribution of π electrons (or p electrons) in the system due to the interaction between atoms in the conjugated system. It is an important electronic effect in organic chemistry. It can change the distribution of electron cloud density in the molecule (coplanarization), reduce the internal energy, average the bond length, increase the refractive index, and make the whole molecule more stable. The research on the structure and properties of these molecules is of great significance both in theory and in practice, so this kind of compounds has aroused people's wide interest.
环庚三烯基配体作为非茂类配体已经广泛的使用在配位化学领域。这种配体是高度共轭的10π电子体系,开创了非苯环芳香族化合物的新领域。近年来,以环庚三烯基为配体的过渡金属配合物的制备一直以来受到科学家们的广泛关注。Saman Damavandi等人最早报道了环庚三烯基过渡钛金属催化剂在烯烃聚合反应中的应用,用于催化乙烯聚合。Philip J.Bailey研究小组合成了镁、铝和铟的环庚三烯基金属有机化合物;Brookhart等人也合成了环庚三烯基配体支撑的镍金属配合物;Peter W.Roesky和Siegfried Blechert等人报道了钙类、锌类环庚三烯基金属配合物,并用其催化了带胺基取代基的端烯烃的氢胺化反应,有很高的活性;Selvarajan Nagendran等人报道合成了锗的环庚三烯基金属配合物,Nathan M.West研究小组成功合成出环庚三烯基配体支撑的铂金属配合物。综上所述,该配体和部分主族金属(如Zn,Mg,Ca,Al等)以及过渡金属(Ni,Ti,Pt等)合成的催化剂已经在有机小分子反应和乙烯聚合中得到了应用。但环庚三烯基金属配合物的制备路线较为复杂,通常是从环庚三烯基配体出发,用KH在-78℃下反应以脱去环庚三烯配体上的氢原子,再加入金属卤化物反应。此过程反应耗时较长,使该方法不具备大规模工业化过程的可能,因此,本领域的技术人员迫切希望找到更为经济、环保且适合工业化的制备环庚三烯基金属化合物的方法。目前,环庚三烯基稀土金属催化剂、制备方法及其在聚合反应中的应用尚未有人报道。Cycloheptatrienyl ligands have been widely used as non-cene ligands in the field of coordination chemistry. This ligand is a highly conjugated 10π electron system, which opens up a new field of non-benzene ring aromatic compounds. In recent years, the preparation of transition metal complexes with cycloheptatrienyl as ligand has been widely concerned by scientists. Saman Damavandi et al. first reported the application of cycloheptatrienyl transition titanium metal catalysts in olefin polymerization to catalyze ethylene polymerization. The Philip J. Bailey research group synthesized cycloheptatrienyl metal organic compounds of magnesium, aluminum and indium; Brookhart et al. also synthesized cycloheptatrienyl ligand-supported nickel metal complexes; Peter W. Roesky and Siegfried Blechert et al. reported calcium and zinc cycloheptatrienyl metal complexes, and used them to catalyze the hydroamination reaction of terminal olefins with amino substituents, which has high activity; Selvarajan Nagendran et al. reported the synthesis of germanium Cycloheptatrienyl metal complexes, Nathan M.West research group successfully synthesized cycloheptatrienyl ligand supported platinum metal complexes. In summary, the catalysts synthesized by this ligand and some main group metals (such as Zn, Mg, Ca, Al, etc.) and transition metals (Ni, Ti, Pt, etc.) have been obtained in organic small molecule reactions and ethylene polymerization. application. However, the preparation route of the cycloheptatrienyl metal complex is relatively complicated, usually starting from the cycloheptatrienyl ligand, reacting with KH at -78°C to remove the hydrogen atom on the cycloheptatriene ligand, and then Add metal halide reaction. This process takes a long time to react, making this method not possible for a large-scale industrial process. Therefore, those skilled in the art are eager to find a method for preparing cycloheptatrienyl metal compounds that is more economical, environmentally friendly and suitable for industrialization. At present, cycloheptatrienyl rare earth metal catalysts, preparation methods and applications in polymerization reactions have not been reported.
发明内容Contents of the invention
本发明的目的之一在于提供一种环庚三烯基稀土金属催化剂;本发明的目的之二在于提供一种环庚三烯基稀土金属催化剂的制备方法;本发明的目的之三在于提供一种环庚三烯基稀土金属催化剂的应用。One of the objects of the present invention is to provide a cycloheptatrienyl rare earth metal catalyst; the second object of the present invention is to provide a preparation method of a cycloheptatrienyl rare earth metal catalyst; the third object of the present invention is to provide a cycloheptatrienyl rare earth metal catalyst Application of a cycloheptatrienyl rare earth metal catalyst.
本发明的目的由以下技术方案实现:The purpose of the present invention is achieved by the following technical solutions:
一种环庚三烯基稀土金属催化剂,所述环庚三烯基稀土金属催化剂结构式结有如下Ⅰ、Ⅱ两种:A cycloheptatrienyl rare earth metal catalyst, the structural formula of the cycloheptatrienyl rare earth metal catalyst has the following two types: I and II:
式Ⅰ、Ⅱ中,R1、R2和R8是与稀土金属相连的引发基团;L1和L2是与稀土金属相连的配位基团;R4、R10和R10’是环庚三烯骨架N原子上的取代基团;R3、R9和R9’是环庚三烯骨架双键上的取代基团;R5、R6、R7、R11、R11’、R12、R12’、R13和R13’是环庚三烯配体骨架上的取代基;Ln1、Ln2是稀土金属;In formulas I and II, R 1 , R 2 and R 8 are initiator groups linked to rare earth metals; L 1 and L 2 are coordination groups linked to rare earth metals; R 4 , R 10 and R 10 ' are Substituent groups on the N atom of the cycloheptatriene skeleton; R 3 , R 9 and R 9 ' are substituent groups on the double bond of the cycloheptatriene skeleton; R 5 , R 6 , R 7 , R 11 , R 11 ', R 12 , R 12 ', R 13 and R 13 'are substituents on the cycloheptatriene ligand skeleton; Ln 1 and Ln 2 are rare earth metals;
其中,R1、R2、R8均优选烷基、三甲基硅基、胺基、亚胺基、烷氧基、苄基、环戊二烯基、茚基、芴基和卤素F、Cl、Br或I中的一种;Among them, R 1 , R 2 and R 8 are all preferably alkyl, trimethylsilyl, amine, imino, alkoxy, benzyl, cyclopentadienyl, indenyl, fluorenyl and halogen F, One of Cl, Br or I;
L1、L2优选磷基配体(如三苯基磷)、醚类配体(如四氢呋喃、乙醚)、中性胺基配体(如吡啶)、咪唑、咔唑、恶唑、DMF中的一种;L 1 and L 2 are preferably phosphorus-based ligands (such as triphenylphosphine), ether ligands (such as tetrahydrofuran, ether), neutral amine-based ligands (such as pyridine), imidazole, carbazole, oxazole, DMF a kind of
R4优选2,6-二甲基苯、2,6-二异丙基苯、2-叔丁基苯、2-甲基-6-叔丁基苯、2,6-二苯基苯、五氟苯、2,6-二溴苯、3,5-三氟甲基苯、2-甲基苯、2-甲基-6-三氟甲基苯、2,6-二氟苯中的一种;R 4 is preferably 2,6-dimethylbenzene, 2,6-diisopropylbenzene, 2-tert-butylbenzene, 2-methyl-6-tert-butylbenzene, 2,6-diphenylbenzene, Pentafluorobenzene, 2,6-dibromobenzene, 3,5-trifluoromethylbenzene, 2-methylbenzene, 2-methyl-6-trifluoromethylbenzene, 2,6-difluorobenzene A sort of;
R10优选异丙基、叔丁基、正丁基中的一种;R is preferably one of isopropyl, tert-butyl and n-butyl;
R3优选2,6-二甲基苯胺、2,6-二异丙基苯胺、2-叔丁基苯胺、2-甲基-6-叔丁基苯胺、2,6-二苯基苯胺、五氟苯胺、2,6-二溴苯胺、3,5-三氟甲基苯胺、2-甲基苯胺、2-甲基-6-三氟甲基苯胺、2,6-二氟苯胺中的一种; R3 is preferably 2,6-dimethylaniline, 2,6-diisopropylaniline, 2-tert-butylaniline, 2-methyl-6-tert-butylaniline, 2,6-diphenylaniline, Pentafluoroaniline, 2,6-dibromoaniline, 3,5-trifluoromethylaniline, 2-methylaniline, 2-methyl-6-trifluoromethylaniline, 2,6-difluoroaniline A sort of;
R9和R9’优选氧原子、异丙胺、叔丁胺中的一种;R 9 and R 9 ' are preferably one of oxygen atom, isopropylamine and tert-butylamine;
R5、R11和R11’优选氢原子、甲基、乙基、烷氧基、异丙基、叔丁基、正丁基、硝基、氨基、碘原子、溴原子、苯基、苄基、腈基、硫苯基、苯胺基、苯酚基、苯硫基和3,5-二氟甲烷苯硫基中的一种;R 5 , R 11 and R 11 ' are preferably hydrogen atom, methyl group, ethyl group, alkoxy group, isopropyl group, tert-butyl group, n-butyl group, nitro group, amino group, iodine atom, bromine atom, phenyl group, benzyl group One of nitrile, thiophenyl, anilino, phenol, thiophenyl and 3,5-difluoromethanephenylthio;
R6、R7优选苯基、苄基、蒽基、萘基、菲基、硫苯基、苯胺基、苯酚基、苯硫基和3,5-二氟甲烷苯硫基中的一种;R 6 and R 7 are preferably one of phenyl, benzyl, anthracenyl, naphthyl, phenanthrenyl, thiophenyl, anilino, phenol, phenylthio and 3,5-difluoromethanephenylthio;
R12、R12’、R13和R13’优选氢原子、甲基、乙基、异丙基、叔丁基、正丁基、烷氧基、腈基、氨基、碘原子、溴原子、硝基、腈基中的一种;R 12 , R 12 ', R 13 and R 13 ' are preferably hydrogen atom, methyl group, ethyl group, isopropyl group, tert-butyl group, n-butyl group, alkoxy group, nitrile group, amino group, iodine atom, bromine atom, One of nitro and nitrile;
Ln1、Ln2优选钪(Sc)、镥(Lu)、钇(Y)、镧(La)、铈(Ce)、镨(Pr)、钕(Nb)、钷(Pm)、钐(Sm)、铕(Eu)、钆(Gd)、铽(Tb)、镝(Dy)、钬(Ho)、铒(Er)、铥(Tm)或镱(Yb);Ln 1 and Ln 2 are preferably scandium (Sc), lutetium (Lu), yttrium (Y), lanthanum (La), cerium (Ce), praseodymium (Pr), neodymium (Nb), promethium (Pm), samarium (Sm) , europium (Eu), gadolinium (Gd), terbium (Tb), dysprosium (Dy), holmium (Ho), erbium (Er), thulium (Tm) or ytterbium (Yb);
一种环庚三烯基稀土金属催化剂的制备方法,所述方法步骤如下:A preparation method of a cycloheptatrienyl rare earth metal catalyst, the method steps are as follows:
(1)制备环庚三烯基配体;(1) preparation of cycloheptatrienyl ligand;
首先,称取环庚三烯酚酮、对甲苯磺酰氯到反应器中,室温下加入良溶剂,良溶剂优选二氯甲烷,开始搅拌混合物,再向混合物中逐滴加入三乙胺,此时就会产生黄色泥浆状物质;另再加入良溶剂稀释反应;在室温下在氮气保护的氛围下,搅拌约32h后,得到化合物a。其中环庚三烯酚酮、对甲苯磺酰氯和三乙胺的摩尔比为1:1:1;First, take tropolone and p-toluenesulfonyl chloride into the reactor, add a good solvent at room temperature, preferably dichloromethane, start stirring the mixture, then add triethylamine dropwise to the mixture, at this time A yellow muddy substance will be produced; another good solvent is added to dilute the reaction; after stirring for about 32 hours at room temperature under the atmosphere of nitrogen protection, compound a is obtained. Wherein the mol ratio of tropolone, p-toluenesulfonyl chloride and triethylamine is 1:1:1;
其次,在低温下,将胺基取代物缓慢滴加入a中;混合物在室温下搅拌过夜。用良溶剂和不良溶剂进行重结晶后,即得到含双键O的产物b;Next, the amine substituent was slowly added dropwise to a at low temperature; the mixture was stirred overnight at room temperature. After recrystallization with a good solvent and a poor solvent, the product b containing double bond O is obtained;
最后,将b产物的CH2Cl2溶液慢慢加入到将Et3OBF4溶液中,在室温下搅拌一定时间后,再把胺基取代物缓缓的滴加入上述反应瓶中,待反应恢复至室温后,搅拌过夜,得到含有目标产物的混合物c;向混合物c中加入良溶剂25~35mL,分层得到水相和有机相,向有机相中加入固体干燥剂5~10g后,过滤,旋干,得到粗产物。再通过柱层析纯化产物的方法得到所述环庚三烯基配体;Finally, slowly add the CH 2 Cl 2 solution of product b into the Et 3 OBF 4 solution, stir at room temperature for a certain period of time, then slowly drop the amino substituent into the above reaction flask, and wait for the reaction to recover After reaching room temperature, stir overnight to obtain a mixture c containing the target product; add 25-35 mL of a good solvent to the mixture c, separate to obtain an aqueous phase and an organic phase, add 5-10 g of a solid desiccant to the organic phase, and filter. Spin dry to get the crude product. The cycloheptatrienyl ligand is obtained by purifying the product through column chromatography;
(2)制备环庚三烯基稀土金属催化剂;(2) prepare cycloheptatrienyl rare earth metal catalyst;
首先,将反应器置于手套箱中,将步骤(1)所述环庚三烯配体逐滴加入到溶有金属源的溶液中,室温下搅拌反应6h,得到混合物,将所述混合物过滤,取所得液体进行浓缩,得到环庚三烯基稀土催化剂粗产品,将所述粗产品重结晶后得到环庚三烯基稀土金属催化剂;First, the reactor is placed in a glove box, the cycloheptatriene ligand described in step (1) is added dropwise to the solution in which the metal source is dissolved, and the reaction is stirred at room temperature for 6 hours to obtain a mixture, which is filtered , taking the obtained liquid and concentrating to obtain a cycloheptatrienyl rare earth catalyst crude product, and recrystallizing the crude product to obtain a cycloheptatrienyl rare earth metal catalyst;
其中,反应温度为20~25℃,环庚三烯基配体与金属源的摩尔比为1:1或2:1;步骤(1)中良溶剂优选二氯甲烷;优选无水硫酸镁(MgSO4)对所述有机相进行干燥;步骤(2)中金属源优选二四氢呋喃-三(三甲基硅甲基)-稀土金属化合物,分子式为[Ln(CH2SiMe3)3(THF)2];Wherein, the temperature of reaction is 20~25 DEG C, and the mol ratio of cycloheptatrienyl ligand and metal source is 1:1 or 2:1; In step (1), the preferred dichloromethane of good solvent; Preferred anhydrous magnesium sulfate ( MgSO 4 ) to dry the organic phase; the metal source in step (2) is preferably ditetrahydrofuran-tris(trimethylsilylmethyl)-rare earth metal compound, the molecular formula is [Ln(CH 2 SiMe 3 ) 3 (THF) 2 ];
一种环庚三烯基稀土金属催化剂的应用,所述环庚三烯基稀土金属催化剂与烷基铝试剂和有机硼盐组成催化体系,用于催化烯烃、炔烃、极性单体的均聚及共聚合反应,或烯烃、炔烃、极性单体分别与CO2的共聚反应;An application of a cycloheptatrienyl rare earth metal catalyst, the cycloheptatrienyl rare earth metal catalyst forms a catalytic system with an alkylaluminum reagent and an organic boron salt, and is used to catalyze the homogeneous reaction of olefins, alkynes, and polar monomers. Polymerization and copolymerization, or copolymerization of olefins, alkynes, and polar monomers with CO2 ;
其中,烷基铝试剂、有机硼盐与环庚三烯基稀土金属催化剂的摩尔比为2~100:1~100:1;烷基铝试剂是分子式为AlR3的烷基铝、分子式为HAlR2的烷基氢化铝、分子式为AlR2Cl的烷基氯化铝或铝氧烷中的一种,R为烷基;Wherein, the molar ratio of the alkylaluminum reagent, organoboron salt and cycloheptatrienyl rare earth metal catalyst is 2-100:1-100:1; the alkylaluminum reagent is an alkylaluminum with a molecular formula of AlR3 and a molecular formula of HAlR 2 alkylaluminum hydride, alkylaluminum chloride or aluminoxane with molecular formula AlR 2 Cl, R is an alkyl group;
所述均聚反应的步骤如下:The steps of the homopolymerization reaction are as follows:
将反应瓶置于手套箱中,在反应瓶中依次加入所述环庚三烯基稀土催化剂,5~10mL良溶剂,烷基铝,烯烃、炔烃或极性单体,有机硼盐,在搅拌下反应0.3~6h后,将反应瓶取出,加入链终止剂,使反应中止;将反应液倒入乙醇中沉降,析出固体物质,将所述固体物质在30℃下用真空干燥箱除去溶剂至恒重,得到均聚产物;The reaction bottle is placed in a glove box, and the cycloheptatrienyl rare earth catalyst, 5-10 mL of good solvent, aluminum alkyl, olefin, alkyne or polar monomer, organoboron salt are added successively in the reaction bottle. After reacting under stirring for 0.3-6h, take out the reaction bottle, add a chain terminator to stop the reaction; pour the reaction solution into ethanol to settle, and precipitate solid matter, and remove the solvent in a vacuum oven at 30°C To constant weight, obtain the homopolymer product;
其中烯烃、炔烃或极性单体,烷基铝试剂,有机硼盐与环庚三烯基稀土催化剂的摩尔比为200~600:2~100:1~100:1;反应温度为25~90℃。Among them, the molar ratio of alkenes, alkynes or polar monomers, alkylaluminum reagents, organic boron salts and cycloheptatrienyl rare earth catalysts is 200-600:2-100:1-100:1; the reaction temperature is 25- 90°C.
所述共聚反应的步骤如下:The steps of the copolymerization reaction are as follows:
将反应瓶置于手套箱中,在反应瓶中依次加入所述环庚三烯基稀土催化剂,1~40mL良溶剂,烷基铝,反应物a或反应物b,有机硼盐,在搅拌下反应3~24h后,将反应瓶取出,加入链终止剂,使反应中止;将反应液倒入乙醇中沉降,析出固体物质,将所述固体物质在30℃下用真空干燥箱除去溶剂至恒重,得到共聚产物;Place the reaction bottle in a glove box, add the cycloheptatrienyl rare earth catalyst, 1 to 40 mL of good solvent, aluminum alkyl, reactant a or reactant b, organoboron salt in turn in the reaction bottle, and stir After reacting for 3 to 24 hours, the reaction bottle was taken out, and a chain terminator was added to terminate the reaction; the reaction solution was poured into ethanol to settle, and a solid substance was precipitated, and the solid substance was removed with a vacuum oven at 30°C until constant Heavy, obtain the copolymerization product;
其中,反应物a或反应物b,烷基铝试剂,有机硼盐与环庚三烯基稀土催化剂的摩尔比为200~5000:2~100:1~100:1;反应温度为25~70℃;反应物a为支链烯烃、环烯烃、炔烃、极性单体中的两种,反应物b为支链烯烃、环烯烃、炔烃、极性单体中的一种和CO2。Wherein, the molar ratio of reactant a or reactant b, alkylaluminum reagent, organoboron salt and cycloheptatrienyl rare earth catalyst is 200-5000:2-100:1-100:1; the reaction temperature is 25-70 ℃; reactant a is two kinds of branched olefins, cycloalkenes, alkynes, and polar monomers, and reactant b is one of branched alkenes, cycloalkenes, alkynes, polar monomers, and CO 2 .
所述烷基铝优选三甲基铝、三乙基铝、三正丙基铝、三正丁基铝、三异丙基铝、三异丁基铝、三己基铝、三环己基铝、三辛基铝、三苯基铝、三对甲苯基铝、三苄基铝、乙基二苄基铝、乙基二对甲苯基铝和二乙基苄基铝中的一种;The aluminum alkyl is preferably trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisopropylaluminum, triisobutylaluminum, trihexylaluminum, tricyclohexylaluminum, tricyclohexylaluminum, One of octyl aluminum, triphenyl aluminum, tri-p-tolyl aluminum, tribenzyl aluminum, ethyl dibenzyl aluminum, ethyl di-p-tolyl aluminum and diethyl benzyl aluminum;
所述烷基氢化铝优选氢化二甲基铝、氢化二乙基铝、氢化二正丙基铝、氢化二正丁基铝、氢化二异丙基铝、氢化二异丁基铝、氢化二戊基铝、氢化二己基铝、氢化二环己基铝、氢化二辛基铝、氢化二苯基铝、氢化二对甲苯基铝、氢化二苄基铝、氢化乙基苄基铝和氢化乙基对甲苯基铝中的一种;The alkyl aluminum hydride is preferably dimethylaluminum hydride, diethylaluminum hydride, di-n-propylaluminum hydride, di-n-butylaluminum hydride, diisopropylaluminum hydride, diisobutylaluminum hydride, dipentylaluminum hydride aluminum hydride, dihexylaluminum hydride, dicyclohexylaluminum hydride, dioctylaluminum hydride, diphenylaluminum hydride, di-p-cresylaluminum hydride, dibenzylaluminum hydride, ethylbenzylaluminum hydride and ethylp- One of the tolyl aluminum;
所述烷基氯化铝优选:氯化二甲基铝、氯化二乙基铝、氯化二正丙基铝、氯化二正丁基铝、氯化二异丙基铝、氯化二异丁基铝、氯化二戊基铝、氯化二己基铝、氯化二环己基铝、氯化二辛基铝、氯化二苯基铝、氯化二对甲苯基铝、氯化二苄基铝、氯化乙基苄基铝和氯化乙基对甲苯基铝中的一种;The alkyl aluminum chloride is preferably: dimethylaluminum chloride, diethylaluminum chloride, di-n-propylaluminum chloride, di-n-butylaluminum chloride, diisopropylaluminum chloride, diisopropylaluminum chloride, Isobutyl aluminum, dipentyl aluminum chloride, dihexyl aluminum chloride, dicyclohexyl aluminum chloride, dioctyl aluminum chloride, diphenyl aluminum chloride, di-p-tolyl aluminum chloride, dichloride One of benzyl aluminum, ethyl benzyl aluminum chloride and ethyl p-tolyl aluminum chloride;
所述铝氧烷优选:甲基铝氧烷、乙基铝氧烷、正丙基铝氧烷和正丁基铝氧烷中的一种;The aluminoxane is preferably: one of methylalumoxane, ethylalumoxane, n-propylalumoxane and n-butylalumoxane;
所述的有机硼盐优选三苯基(甲基)-四(五氟苯)硼盐([Ph3C][B(C6F5)4])、苯基-二甲基氨基-四(五氟苯)硼盐([PhMe2NH][B(C6F5)4])、苯基-二甲基氨基-四苯基硼盐([PhMe2NH][BPh4])或三(五氟苯)硼盐(B(C6F5)3)中的一种;The organoboron salt is preferably triphenyl(methyl)-tetrakis(pentafluorophenyl)boron salt ([Ph 3 C][B(C 6 F 5 ) 4 ]), phenyl-dimethylamino-tetrakis (Pentafluorophenyl) boron salt ([PhMe 2 NH][B(C 6 F 5 ) 4 ]), phenyl-dimethylamino-tetraphenyl boron salt ([PhMe 2 NH][BPh 4 ]) or One of tris(pentafluorophenyl)boron salts (B(C 6 F 5 ) 3 );
所述支链烯烃优选乙烯、丙烯、1-丁烯、1-戊烯、4-甲基-1-戊烯、1-己烯、1-庚烯、1-辛烯、1-癸烯、1-十二碳烯、1-十四碳烯、1-十六碳烯、1-二十碳烯,苯乙烯、α-甲基苯乙烯、3-氯甲基苯乙烯、1,3-丁二烯、异戊二烯、1,3-环己二烯、1,5-戊二烯、1,6-己二烯和二乙烯基苯中的一种;The branched olefins are preferably ethylene, propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-eicosene, styrene, α-methylstyrene, 3-chloromethylstyrene, 1,3- One of butadiene, isoprene, 1,3-cyclohexadiene, 1,5-pentadiene, 1,6-hexadiene and divinylbenzene;
所述环烯烃优选降冰片烯、极性降冰片烯、降冰片二烯、亚乙基降冰片烯、苯基降冰片烯、乙烯基降冰片烯和双环戊二烯中的一种;The cycloolefin is preferably one of norbornene, polar norbornene, norbornadiene, ethylidene norbornene, phenyl norbornene, vinyl norbornene and dicyclopentadiene;
所述的炔烃优选乙炔、苯乙炔、对苯乙炔和二乙炔基芳烃中的一种;The alkyne is preferably one of acetylene, phenylacetylene, p-phenyleneacetylene and diethynyl arenes;
所述的极性单体分为环氧烷烃和内酯,其中环氧烷烃优选环氧乙烷、环氧丙烷、1,2-环氧丁烷、2,3-环氧丁烷、异环氧丁烷、环氧氯丙烷、环氧溴丙烷、甲基缩水甘油醚、烯丙基缩水甘油醚、丁基缩水甘油醚、2-乙基亚己基缩水甘油醚、三氟环氧丙烷,内酯为ε-己内酯、β-丁内酯、δ-戊内酯、丙交酯、乙交酯和3-甲基-乙交酯中的一种;The polar monomers are divided into alkylene oxides and lactones, wherein alkylene oxides are preferably ethylene oxide, propylene oxide, 1,2-butylene oxide, 2,3-butylene oxide, heterocyclic Oxybutylene, epichlorohydrin, epibromohydrin, methyl glycidyl ether, allyl glycidyl ether, butyl glycidyl ether, 2-ethylhexylidene glycidyl ether, trifluoropropylene oxide, internal The ester is one of ε-caprolactone, β-butyrolactone, δ-valerolactone, lactide, glycolide and 3-methyl-glycolide;
所述链终止剂优选含5%2,6-二叔丁基-4-甲基苯酚的乙醇,以乙醇的体积为100%计,其中,2,6-二叔丁基-4-甲基苯酚所占体积比为5%;良溶剂优选甲苯。The chain terminator preferably contains 5% ethanol of 2,6-di-tert-butyl-4-methylphenol, and the volume of ethanol is 100%, wherein, 2,6-di-tert-butyl-4-methyl The volume ratio of phenol is 5%; the good solvent is preferably toluene.
有益效果Beneficial effect
(1)本发明所述的环庚三烯基稀土金属催化剂,是以环庚三烯酚酮为初始原料,原料价廉易得,且易于修饰;(1) The cycloheptatrienyl rare earth metal catalyst of the present invention is based on tropolone as the initial raw material, and the raw material is cheap and easy to obtain, and is easy to modify;
(2)本发明所述的环庚三烯基稀土金属催化剂的制备方法,经济效率高、环保性好,适合工业化生产;(2) The preparation method of the cycloheptatrienyl rare earth metal catalyst of the present invention has high economic efficiency and good environmental protection, and is suitable for industrialized production;
(3)本发明所述的环庚三烯基稀土金属催化剂、烷基铝试剂以及有机硼盐组成的催化体系,可进行支链烯烃、环烯烃、炔烃、极性单体的均聚及共聚反应或支链烯烃、环烯烃、炔烃、极性单体与CO2的共聚反应,得到一系列具有特定结构的新型聚合材料;(3) The catalytic system formed by cycloheptatrienyl rare earth metal catalyst, alkylaluminum reagent and organic boron salt according to the present invention can carry out homopolymerization and Copolymerization or copolymerization of branched olefins, cyclic olefins, alkynes, polar monomers and CO2 to obtain a series of new polymer materials with specific structures;
(4)本发明所述的环庚三烯基稀土金属催化剂,在催化L-丙交酯和ε-己内酯聚合时,能使ε-己内酯的均聚的产率达到74.9%,对L-丙交酯的均聚的产率可达100%。(4) The cycloheptatrienyl rare earth metal catalyst of the present invention can make the homopolymerization yield of ε-caprolactone reach 74.9% when catalyzing the polymerization of L-lactide and ε-caprolactone, The yield of homopolymerization of L-lactide can reach 100%.
(5)本发明所述的环庚三烯基稀土金属催化剂,在催化异戊二烯聚合时,产率可以达到100%,顺1,4-结构的选择性最高可达94.34%。这是一种尚未报道的新型异戊二烯橡胶材料,对其理化性质的进一步研究将会有助于为其寻找合适的应用用途。(5) When the cycloheptatrienyl rare earth metal catalyst of the present invention catalyzes the polymerization of isoprene, the yield can reach 100%, and the selectivity of the cis 1,4-structure can reach up to 94.34%. This is a new type of isoprene rubber material that has not been reported yet. Further research on its physical and chemical properties will help to find suitable applications for it.
附图说明Description of drawings
图1为环庚三烯基钪催化剂的X-射线单晶衍射表征的晶体结构图。Fig. 1 is a crystal structure diagram characterized by X-ray single crystal diffraction of cycloheptatrienyl scandium catalyst.
具体实施方式detailed description
下面结合附图和具体实施例对本发明做进一步说明,但不限于此。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments, but is not limited thereto.
以下实施例中提到的主要试剂信息见表1;主要仪器与设备信息见表2。The main reagent information mentioned in the following examples is shown in Table 1; the main instruments and equipment information are shown in Table 2.
表1Table 1
表2Table 2
以下实施例中聚合活性由公式Activity=(m·yeild)/(ncat·time)计算得出。其中,Activity为活性聚合,单位为kg·mol-1·h-1,m为支链烯烃、环烯烃、炔烃、极性单体或CO2的质量,yield为产率,ncat为催化剂物质的量,time为聚合所用时间。In the following examples, the polymerization activity is calculated by the formula Activity=(m·yeild)/(n cat ·time). Among them, Activity is active polymerization, the unit is kg mol -1 h -1 , m is the mass of branched alkenes, cycloalkenes, alkynes, polar monomers or CO 2 , yield is the yield, and n cat is the catalyst The amount of substance, time is the time used for polymerization.
聚异戊二烯微观结构可以由1H-NMR和13C-NMR谱图给出,选择性具体计算公式如下:The microstructure of polyisoprene can be given by 1 H-NMR and 13 C-NMR spectra, and the specific calculation formula of selectivity is as follows:
(1)1,4-聚异戊二烯的选择性(所占比例):(1) Selectivity (proportion) of 1,4-polyisoprene:
Mol 1,4-IP%={IH1/(IH1+0.5IH2)}×100Mol 1,4-IP%={I H1 /(I H1 +0.5I H2 )}×100
(2)3,4-聚异戊二烯的选择性(所占比例):(2) Selectivity (proportion) of 3,4-polyisoprene:
Mol 3,4-IP%={0.5IH2/(IH1+0.5IH2)}×100Mol 3,4-IP%={0.5I H2 /(I H1 +0.5I H2 )}×100
(3)顺1,4-聚异戊二烯的选择性(所占比例):(3) Selectivity (proportion) of cis 1,4-polyisoprene:
Mol cis-1,4-IP%={IC1/(IC1+IC2+IC3)}×100Mol cis-1,4-IP%={I C1 /(I C1 +I C2 +I C3 )}×100
(4)反1,4-聚异戊二烯的选择性(所占比例):(4) Selectivity (proportion) of anti-1,4-polyisoprene:
Mol trans-1,4-IP%={IC3/(IC1+IC2+IC3)}×100Mol trans-1,4-IP%={I C3 /(I C1 +I C2 +I C3 )}×100
(5)3,4-聚异戊二烯的选择性(所占比例):(5) Selectivity (proportion) of 3,4-polyisoprene:
Mol 3,4-IP%={IC2/(IC1+IC2+IC3)}×100Mol 3,4-IP%={I C2 /(I C1 +I C2 +I C3 )}×100
其中,IP为聚异戊二烯,IH1为1H谱中5.13ppm处的积分;IH2为1H谱中4.72ppm处的积分;IC1为13C谱中23.2ppm处的积分;IC2为13C谱中18.5ppm处的积分;IC3为13C谱中15.9ppm处的积分。Wherein, IP is polyisoprene, I H1 is the integral at 5.13ppm in the 1 H spectrum; I H2 is the integral at 4.72ppm in the 1H spectrum; I C1 is the integral at 23.2ppm in the 13 C spectrum; I C2 is the integral at 18.5 ppm in the 13 C spectrum; IC3 is the integral at 15.9 ppm in the 13 C spectrum.
实施例1Example 1
(1)制备环庚三烯基配体(1) Preparation of cycloheptatrienyl ligand
首先,称取环庚三烯酚酮5.3g(43mmol)和对甲苯磺酰氯8.2g(43mmol)到反应器中,室温下加入60mL二氯甲烷,开始搅拌混合物,再向混合物中逐滴加入6mL(43mmol)三乙胺,此时就会产生黄色泥浆状物质。另再加入60mL二氯甲烷。在室温下在氮气保护的氛围下,搅拌约32h后,得到化合物a。First, weigh 5.3 g (43 mmol) of tropolone and 8.2 g (43 mmol) of p-toluenesulfonyl chloride into the reactor, add 60 mL of dichloromethane at room temperature, start stirring the mixture, and then add 6 mL of (43mmol) triethylamine, this moment will produce yellow muddy substance. Another 60 mL of dichloromethane was added. Compound a was obtained after stirring for about 32 h at room temperature under an atmosphere of nitrogen protection.
其次,在低温下,将异丙胺(60mL)缓慢滴加入a(10.92g,40.0mmol)中。混合物在室温下搅拌过夜后,减压旋蒸,得到的物质用2mol/L NaOH(60mL)和CH2Cl2(120mL)溶解,分层,分离出有机相。水相再用CH2Cl2(120mL)萃取2次。合并有机相,用20mL浓盐水洗涤,并用无水MgSO4干燥,抽滤,滤液旋干,得到的固体用CH2Cl2和正己烷进行重结晶后,得到黄色固体b,即为环庚三烯基配体,产率为80.9%。Next, isopropylamine (60 mL) was slowly added dropwise into a (10.92 g, 40.0 mmol) at low temperature. After the mixture was stirred overnight at room temperature, it was rotary evaporated under reduced pressure, and the obtained substance was dissolved in 2 mol/L NaOH (60 mL) and CH 2 Cl 2 (120 mL), separated into layers, and the organic phase was separated. The aqueous phase was extracted 2 more times with CH2Cl2 (120 mL). The organic phases were combined, washed with 20 mL of concentrated brine, dried with anhydrous MgSO 4 , filtered with suction, and the filtrate was spin-dried, and the obtained solid was recrystallized with CH 2 Cl 2 and n-hexane to obtain a yellow solid b, which was cycloheptane Alkenyl ligand, yield 80.9%.
(2)制备环庚三烯基钪催化剂(2) Preparation of Cycloheptatrienyl Scandium Catalyst
首先,将反应器置于手套箱中,将步骤(1)制备的环庚三烯配体(665.9mg,4.08mmol)逐滴加入到溶有Sc(CH2SiMe3)3(thf)2(920mg,2.04mmol)的甲苯溶液中,在搅拌下反应6h,得到混合物c;其中,反应温度为25℃;First, the reactor was placed in a glove box, and the cycloheptatriene ligand (665.9 mg, 4.08 mmol) prepared in step (1) was added dropwise to a solution of Sc(CH 2 SiMe 3 ) 3 (thf) 2 ( 920mg, 2.04mmol) of toluene solution, reacted for 6h under stirring to obtain mixture c; wherein, the reaction temperature was 25°C;
其次,将所述混合物c过滤,取所得液体进行浓缩,得到环庚三烯基钪催化剂粗产品,将所述粗产品重结晶后得到黄色粉末0.720g,即为环庚三烯基钪催化剂d,产率为65%。如附图所示为环庚三烯基钪催化剂d的X-射线单晶衍射表征的晶体结构图。Next, the mixture c was filtered, and the resulting liquid was concentrated to obtain a crude cycloheptatrienyl scandium catalyst product, which was recrystallized to obtain 0.720 g of a yellow powder, which was cycloheptatrienyl scandium catalyst d , the yield was 65%. As shown in the accompanying drawing, it is a crystal structure diagram characterized by X-ray single crystal diffraction of cycloheptatrienyl scandium catalyst d.
以下实施例5~实施例11以及实施例16~实施例18为实施例1所述的环庚三烯基钪催化剂d的应用。The following examples 5 to 11 and examples 16 to 18 are applications of the cycloheptatrienyl scandium catalyst d described in example 1.
实施例2Example 2
(1)制备环庚三烯基配体(1) Preparation of cycloheptatrienyl ligand
首先,称取环庚三烯酚酮5.3g(43mmol)和对甲苯磺酰氯8.2g(43mmol)到反应器中,室温下加入60mL二氯甲烷,再向混合物中逐滴加入4.4g(6mL,43mmol)三乙胺,另再加入60mL二氯甲烷。在室温氮气保护下,搅拌约32h后,得到化合物a。化合物b的操作同实施例1。其次,将b产物(1.37g,9.20mmol)的CH2Cl2溶液慢慢加入到将Et3OBF4(1.75g,9.21mmol)溶液中,在室温下搅拌3h后,点板,直至新产物点不再发生变化时,将反应冷却至0℃,再把异丙胺(20mL)缓缓的滴加入上述反应瓶中,待反应恢复至室温后,搅拌过夜,得到含有目标产物的混合物e。减压旋蒸后的油状物质用NaOH(10mL)和CH2Cl2(20mL)溶解,分离有机相。水相用CH2Cl2(20mL)萃取2次。合并有机相,用20mL浓盐水洗涤,并用无水MgSO4干燥。抽滤,旋干。得到粗产物。再通过柱层析纯化产物的方法得到1.39g所述环庚三烯基配体f,产率为47.9%。First, weigh 5.3 g (43 mmol) of tropolone and 8.2 g (43 mmol) of p-toluenesulfonyl chloride into the reactor, add 60 mL of dichloromethane at room temperature, and then add 4.4 g (6 mL, 43mmol) triethylamine, and another 60mL of dichloromethane was added. Under the protection of nitrogen at room temperature, after stirring for about 32 h, compound a was obtained. The operation of compound b is the same as in Example 1. Next, slowly add the CH 2 Cl 2 solution of product b (1.37g, 9.20mmol) into the Et 3 OBF 4 (1.75g, 9.21mmol) solution, stir at room temperature for 3h, and spot the plate until the new product When the point no longer changed, the reaction was cooled to 0°C, and then isopropylamine (20 mL) was slowly added dropwise into the above reaction flask. After the reaction returned to room temperature, it was stirred overnight to obtain a mixture e containing the target product. The oily substance after rotary evaporation under reduced pressure was dissolved in NaOH (10 mL) and CH 2 Cl 2 (20 mL), and the organic phase was separated. The aqueous phase was extracted twice with CH2Cl2 ( 20 mL). The organic phases were combined, washed with 20 mL of concentrated brine, and dried over anhydrous MgSO 4 . Suction filter and spin dry. The crude product was obtained. The product was purified by column chromatography to obtain 1.39 g of the cycloheptatrienyl ligand f with a yield of 47.9%.
(2)制备环庚三烯基钪催化剂(2) Preparation of Cycloheptatrienyl Scandium Catalyst
首先,将反应器置于手套箱中,将步骤(1)制备的环庚三烯基配体f(613.0mg,3mmol)逐滴加入到溶有Sc(CH2SiMe3)3(thf)2(676.2mg,1.5mmol)的甲苯溶液中,在搅拌下反应6h,得到混合物g;其中,反应温度为25℃;First, the reactor was placed in the glove box, and the cycloheptatrienyl ligand f (613.0mg, 3mmol) prepared in step (1) was added dropwise to the dissolved Sc(CH 2 SiMe 3 ) 3 (thf) 2 (676.2mg, 1.5mmol) in a toluene solution, reacted for 6h under stirring to obtain a mixture g; wherein, the reaction temperature was 25°C;
其次,将所述混合物g过滤后,进行浓缩,得到环庚三烯基钪催化剂粗产品,将所述粗产品重结晶后得到黄色粉末0.530g,即为环庚三烯基钪催化剂h,产率为58%。Next, after the mixture g is filtered, it is concentrated to obtain a crude product of the cycloheptatrienyl scandium catalyst, and the crude product is recrystallized to obtain 0.530 g of a yellow powder, which is the cycloheptatrienyl scandium catalyst h, producing The rate is 58%.
以下实施例12~15为实施例2所述的环庚三烯基钪催化剂h的聚合应用。The following examples 12-15 are the polymerization application of cycloheptatrienyl scandium catalyst h described in example 2.
实施例3Example 3
(1)制备环庚三烯基配体(1) Preparation of cycloheptatrienyl ligand
化合物a、b的操作同实施例1。之后,将b产物(1.37g,9.20mmol)的CH2Cl2溶液慢慢加入到将Et3OBF4(1.75g,9.21mmol)溶液中,在室温下搅拌3h后,点板,确定有新的产物生成,直至新产物点不再发生变化时,将反应冷却至0℃,再把异丙胺(20mL)以1s/滴的速度缓缓的滴加入上述反应瓶中,待反应恢复至室温后,搅拌过夜,得到含有目标产物的混合物e。再通过柱层析纯化产物的方法得到1.39g所述环庚三烯基配体f,产率为47.9%。The operation of compounds a and b is the same as in Example 1. Afterwards, the CH 2 Cl 2 solution of product b (1.37g, 9.20mmol) was slowly added to the Et 3 OBF 4 (1.75g, 9.21mmol) solution, and after stirring at room temperature for 3h, spot the plate to confirm that there was new The product is formed until the new product point no longer changes, the reaction is cooled to 0°C, and then isopropylamine (20mL) is slowly added dropwise at a rate of 1s/drop into the above reaction flask, and the reaction is returned to room temperature , stirred overnight to obtain mixture e containing the desired product. The product was purified by column chromatography to obtain 1.39 g of the cycloheptatrienyl ligand f with a yield of 47.9%.
(2)制备环庚三烯基镥催化剂(2) Preparation of Cycloheptatrienyl Lutetium Catalyst
首先,将反应器置于手套箱中,将步骤(1)制备的环庚三烯基配体f(326.9mg,3.0mmol)逐滴加入到溶有Lu(CH2SiMe3)3(thf)2(676.2mg,1.5mmol)的甲苯溶液中,在搅拌下反应6h,得到混合物i;其中,反应温度为25℃;First, the reactor was placed in the glove box, and the cycloheptatrienyl ligand f (326.9 mg, 3.0 mmol) prepared in step (1) was added dropwise to the solution of Lu(CH 2 SiMe 3 ) 3 (thf) 2 (676.2mg, 1.5mmol) in toluene solution, reacted for 6h under stirring to obtain mixture i; wherein, the reaction temperature was 25°C;
其次,将所述混合物i过滤后,进行浓缩,得到环庚三烯基镥催化剂粗产品,将所述粗产品在-33℃下重结晶后得到0.699g的环庚三烯基镥催化剂j,产率为63%。Next, after the mixture i was filtered, it was concentrated to obtain a crude cycloheptatrienyllutetium catalyst product, which was recrystallized at -33°C to obtain 0.699g of cycloheptatrienyllutetium catalyst j, The yield was 63%.
实施例4Example 4
(1)制备环庚三烯基配体(1) Preparation of cycloheptatrienyl ligand
化合物a的操作同实施例1。之后,在0℃下,将异丙胺(60mL)缓慢滴加入a(10.92g,40.0mmol)中。混合物在室温下搅拌过夜。后处理得到的固体用CH2Cl2和正己烷进行重结晶后,得到黄色固体b。最后,将b产物(1.37g,9.20mmol)的CH2Cl2溶液慢慢加入到将Et3OBF4(1.75g,9.21mmol)溶液中,在室温下搅拌3h后,点板,确定有新的产物生成时,将反应冷却至0℃,再把异丙胺(20mL)缓缓的滴加入上述反应瓶中,待反应恢复至室温后,搅拌过夜,得到含有目标产物的混合物e。再通过柱层析纯化产物的方法得到1.39g所述环庚三烯基配体f,产率为47.9%。The operation of compound a is the same as in Example 1. After that, isopropylamine (60 mL) was slowly added dropwise into a (10.92 g, 40.0 mmol) at 0°C. The mixture was stirred overnight at room temperature. After recrystallization of the obtained solid with CH 2 Cl 2 and n-hexane, a yellow solid b was obtained. Finally, the CH 2 Cl 2 solution of product b (1.37g, 9.20mmol) was slowly added to the Et 3 OBF 4 (1.75g, 9.21mmol) solution, and after stirring at room temperature for 3h, spot the plate to confirm that there was new When the product was formed, the reaction was cooled to 0°C, and then isopropylamine (20 mL) was slowly added dropwise into the reaction flask. After the reaction returned to room temperature, it was stirred overnight to obtain a mixture e containing the target product. The product was purified by column chromatography to obtain 1.39 g of the cycloheptatrienyl ligand f with a yield of 47.9%.
(2)制备环庚三烯基钇催化剂(2) Preparation of Cycloheptatrienyl Yttrium Catalyst
首先,将反应器置于手套箱中,将步骤(1)制备的环庚三烯基配体f(1175.2mg,4.7mmol)逐滴加入到溶有Y(CH2SiMe3)3(thf)2(1162.8mg,2.4mmol)的甲苯溶液中,在搅拌下反应6h,得到混合物k;其中,反应温度为25℃;First, the reactor was placed in the glove box, and the cycloheptatrienyl ligand f (1175.2 mg, 4.7 mmol) prepared in step (1) was added dropwise to the solution of Y(CH 2 SiMe 3 ) 3 (thf) 2 (1162.8mg, 2.4mmol) in toluene solution, reacted for 6h under stirring to obtain mixture k; wherein, the reaction temperature was 25°C;
其次,将所述混合物k过滤后,进行浓缩,得到环庚三烯基镥催化剂粗产品,将所述粗产品在-33℃下重结晶后得到0.989g的环庚三烯基镥催化剂l,产率为63%。Next, after filtering the mixture k, it was concentrated to obtain a crude cycloheptatrienyllutetium catalyst product, which was recrystallized at -33°C to obtain 0.989g of cycloheptatrienyllutetium catalyst 1, The yield was 63%.
实施例5Example 5
将反应器置于手套箱中,向茄瓶中依次加入20μmol环庚三烯基钪催化剂d,40μmol的iPrOH,加入2mL THF,室温搅拌10~30min后,将3mL含8mmol L-丙交酯的THF溶液,再加入催化剂混合物中,搅拌反应2.5h,反应温度25℃,待溶液变得粘稠后,加入体积分数10%的HCl的乙醇溶液中止反应,再倒入乙醇中沉降,过滤,洗涤得到白色聚合物,将所述固体物质在30℃下真空干燥,除去溶剂至恒重,得到聚丙交酯,净重0.055g,转化率5.8%,聚合活性为1.64kg·mol-1·h-1;GPC分析聚丙交酯的数均分子量Mn=23×104,分子量分布Mw/Mn=1.58。Put the reactor in the glove box, add 20 μmol of cycloheptatrienyl scandium catalyst d, 40 μmol of iPrOH to the eggplant bottle, add 2mL of THF, stir at room temperature for 10-30min, and then add 3mL containing 8mmol of L-lactide Add THF solution into the catalyst mixture, stir and react for 2.5h, the reaction temperature is 25°C, after the solution becomes viscous, add 10% HCl ethanol solution by volume fraction to stop the reaction, then pour into ethanol to settle, filter, The white polymer was obtained by washing, and the solid was vacuum-dried at 30° C., and the solvent was removed to a constant weight to obtain polylactide, with a net weight of 0.055 g, a conversion rate of 5.8%, and a polymerization activity of 1.64 kg·mol -1 ·h - 1 ; GPC analysis of polylactide has a number average molecular weight M n =23×10 4 , and a molecular weight distribution M w /M n =1.58.
实施例6Example 6
将反应器置于手套箱中,向茄瓶中依次加入20μmol环庚三烯基钪催化剂d,40μmol的EtONa,加入2mL的CH2Cl2,室温搅拌10~30min后,将3mL含8mmol L-丙交酯的CH2Cl2溶液,再加入催化剂混合物中,搅拌反应2.5h,反应温度25℃,其余操作同实施例5,得到聚丙交酯,净重1.179g,转化率为100%,聚合活性为23.58kg·mol-1·h-1;GPC分析聚丙交酯的数均分子量Mn=15×104,分子量分布Mw/Mn=1.31。Put the reactor in a glove box, add 20 μmol of cycloheptatrienyl scandium catalyst d, 40 μmol of EtONa, and 2 mL of CH 2 Cl 2 into the eggplant bottle, and stir at room temperature for 10 to 30 minutes, then add 3 mL of 8 mmol L- The CH2Cl2 solution of lactide was added to the catalyst mixture, stirred and reacted for 2.5h, the reaction temperature was 25°C, and the rest of the operations were the same as in Example 5 to obtain polylactide, with a net weight of 1.179g, a conversion rate of 100%, and a polymerization activity of It is 23.58 kg·mol -1 ·h -1 ; the number average molecular weight of polylactide M n =15×10 4 by GPC analysis, and the molecular weight distribution M w /M n =1.31.
实施例7Example 7
将反应器置于手套箱中,向茄瓶中依次加入20μmol环庚三烯基钪催化剂d,40μmol的EtONa,加入2mL的THF,搅拌10~30min后,将3mL含8mmolε-己内酯的THF溶液,再加入催化剂混合物中,搅拌反应2.5h,其余操作同实施例5,得到聚己内酯0.683g,转化率为74.9%,聚合活性为13.68kg·mol-1·h-1;GPC分析聚己内酯的数均分子量Mn=9×104,分子量分布Mw/Mn=1.69。Put the reactor in a glove box, add 20 μmol of cycloheptatrienyl scandium catalyst d, 40 μmol of EtONa, and 2 mL of THF to the eggplant bottle, and stir for 10 to 30 minutes, then add 3 mL of THF containing 8 mmol ε-caprolactone solution, and then added to the catalyst mixture, stirred and reacted for 2.5h, and the rest of the operations were the same as in Example 5 to obtain 0.683g of polycaprolactone, with a conversion rate of 74.9%, and a polymerization activity of 13.68kg·mol -1 ·h -1 ; GPC analysis The number average molecular weight M n of polycaprolactone = 9×10 4 , and the molecular weight distribution M w /M n = 1.69.
实施例8Example 8
将反应器置于手套箱中,向茄瓶中依次加入20μmol环庚三烯基钪催化剂d,40μmol的EtONa,加入2mL的CH2Cl2,搅拌10~30min后,将3mL含4mmol的L-丙交酯和4mmol的ε-己内酯的CH2Cl2溶液,再加入催化剂混合物中,搅拌反应4h,其余操作同实施例5,得到L-丙交酯和ε-己内酯的共聚物,净重0.859g,聚合活性为34.36kg·mol-1·h-1;GPC分析共聚物的数均分子量Mn=8×104,分子量分布Mw/Mn=1.33。Put the reactor in a glove box, add 20 μmol of cycloheptatrienyl scandium catalyst d, 40 μmol of EtONa, and 2 mL of CH 2 Cl 2 into the eggplant bottle, and stir for 10 to 30 minutes, then add 3 mL of 4 mmol of L- Lactide and 4 mmol of ε-caprolactone in CH 2 Cl 2 solution were added to the catalyst mixture, stirred for 4 hours, and the remaining operations were the same as in Example 5 to obtain a copolymer of L-lactide and ε-caprolactone , net weight 0.859g, polymerization activity 34.36kg·mol -1 ·h -1 ; GPC analysis of the number average molecular weight of the copolymer M n =8×10 4 , molecular weight distribution M w /M n =1.33.
实施例9Example 9
将反应器置于手套箱中,向茄瓶中依次加入25μmol环庚三烯基钪催化剂d,5mL甲苯,50μmol AliBu3,5mmol苯乙炔及25μmol[PhNHMe2][B(C6F5)4],在50℃下反应0.3h后将茄瓶取出,加入30mL含5%2,6-二叔丁基-4-甲基苯酚的乙醇,使反应中止;将反应液用乙醇进行沉降,析出白色固体物质,将所述固体物质在30℃下真空干燥,除去溶剂至恒重,得到聚苯乙炔,净重0.29g,转化率57%;GPC分析聚苯乙炔的数均分子量Mn=2×104,分子量分布Mw/Mn=1.73。Put the reactor in the glove box, add 25 μmol of cycloheptatrienyl scandium catalyst d, 5 mL of toluene, 50 μmol of Al i Bu 3 , 5 mmol of phenylacetylene and 25 μmol of [PhNHMe 2 ][B(C 6 F 5 ) 4 ], after reacting at 50°C for 0.3h, take out the eggplant bottle, add 30mL of ethanol containing 5% 2,6-di-tert-butyl-4-methylphenol to stop the reaction; settle the reaction solution with ethanol , precipitated a white solid substance, the solid substance was vacuum-dried at 30° C., and the solvent was removed to a constant weight to obtain polyphenylene vinylene with a net weight of 0.29 g and a conversion rate of 57%; the number average molecular weight M n of polyphenylene vinylene was analyzed by GPC = 2×10 4 , molecular weight distribution M w /M n = 1.73.
实施例10Example 10
将反应器置于手套箱中,向茄瓶中依次加入25μmol环庚三烯钪催化剂d,5mL甲苯,50μmol AlMe3,5mmol环氧丙烷及25μmol[Ph3C][B(C6F5)4],反应时间5h,反应温度50℃,其余操作同实施例9,得到聚环氧丙烷,净重0.26g,转化率90%;GPC分析聚环氧丙烷的数均分子量Mn=17×104,分子量分布Mw/Mn=1.62。Put the reactor in the glove box, add 25 μmol scandium cycloheptatriene catalyst d, 5 mL toluene, 50 μmol AlMe 3 , 5 mmol propylene oxide and 25 μmol [Ph 3 C][B(C 6 F 5 ) 4 ], reaction time 5h, reaction temperature 50 ℃, all the other operations are with embodiment 9, obtain polypropylene oxide, net weight 0.26g, transformation efficiency 90%; GPC analyzes the number average molecular weight M n of polypropylene oxide =17 * 10 4 , molecular weight distribution M w /M n = 1.62.
实施例11Example 11
将反应器置于手套箱中,向茄瓶中依次加入21μmol环庚三烯基钪催化剂d,25mL甲苯,42μmol AliBu3,53mmol降冰片烯,53mmol 1,4-丁二烯,及21μmol[Ph3C][B(C6F5)4],反应时间3h,反应温度25℃,其余操作同实施例9,得到降冰片烯与1,4-丁二烯的共聚物,转化率79%;GPC分析共聚物的数均分子量Mn=3.5×104,分子量分布Mw/Mn=1.69。The reactor was placed in a glove box, and 21 μmol of cycloheptatrienyl scandium catalyst d, 25 mL of toluene, 42 μmol of Al i Bu 3 , 53 mmol of norbornene, 53 mmol of 1,4-butadiene, and 21 μmol of [Ph 3 C][B(C 6 F 5 ) 4 ], the reaction time is 3h, the reaction temperature is 25°C, and the rest of the operations are the same as in Example 9 to obtain a copolymer of norbornene and 1,4-butadiene, the conversion rate 79%; GPC analysis of the number average molecular weight of the copolymer M n =3.5×10 4 , molecular weight distribution M w /M n =1.69.
实施例12Example 12
将反应器置于手套箱中,向茄瓶中依次加入25μmol环庚三烯基钪催化剂h,5mL甲苯,50μmol AliBu3,15mmol异戊二烯及25μmol[Ph3C][B(C6F5)4],反应时间为6h,反应温度25℃,其余操作同实施例9,得到聚异戊二烯,净重0.714g,转化率70%,聚合活性为4.8kg·mol-1·h-1;GPC分析聚异戊二烯的数均分子量为Mn=10×103,分子量分布Mw/Mn=1.54;顺1,4-聚合选择性为84%。The reactor was placed in a glove box, and 25 μmol cycloheptatrienyl scandium catalyst h, 5 mL toluene, 50 μmol Al i Bu 3 , 15 mmol isoprene and 25 μmol [Ph 3 C][B(C 6 F 5 ) 4 ], the reaction time was 6 hours, the reaction temperature was 25°C, and the rest of the operations were the same as in Example 9 to obtain polyisoprene with a net weight of 0.714 g, a conversion rate of 70%, and a polymerization activity of 4.8 kg·mol -1 · h -1 ; GPC analysis showed that the number average molecular weight of polyisoprene was Mn=10×10 3 , and the molecular weight distribution M w /M n =1.54; the cis 1,4-polymerization selectivity was 84%.
实施例13Example 13
将反应器置于手套箱中,向茄瓶中依次加入25μmol环庚三烯基钪催化剂h,5mL甲苯,50μmol AliBu3,5mmol异戊二烯及25μmol[Ph3C][B(C6F5)4],反应时间为6h,反应温度25℃,其余操作同实施例9,得到聚异戊二烯,净重0.335g,转化率98.5%,聚合活性为2.2kg·mol-1·h-1;GPC分析聚异戊二烯的数均分子量为Mn=15×103,分子量分布Mw/Mn=1.76;顺1,4-聚合选择性为94.34%。The reactor was placed in a glove box, and 25 μmol cycloheptatrienyl scandium catalyst h, 5 mL toluene, 50 μmol Al i Bu 3 , 5 mmol isoprene and 25 μmol [Ph 3 C][B(C 6 F 5 ) 4 ], the reaction time was 6 hours, the reaction temperature was 25°C, and the rest of the operations were the same as in Example 9 to obtain polyisoprene with a net weight of 0.335 g, a conversion rate of 98.5%, and a polymerization activity of 2.2 kg·mol -1 · h -1 ; GPC analysis showed that the number average molecular weight of polyisoprene was Mn=15×10 3 , and the molecular weight distribution M w /M n =1.76; the cis 1,4-polymerization selectivity was 94.34%.
实施例14Example 14
将反应器置于手套箱中,向茄瓶中依次加入25μmol环庚三烯基钪催化剂h,10mL甲苯,2.5mmol AliBu3,5mmol异戊二烯及2.5mmol[PhNHMe2][B(C6F5)4],反应时间3h,反应温度25℃,其余操作同实施例9,得到聚异戊二烯,净重0.306g,转化率90%,聚合活性为4.1kg·mol-1·h-1;GPC分析聚异戊二烯的数均分子量为Mn=18×103,分子量分布Mw/Mn=1.98;顺1,4-聚合选择性89%。The reactor was placed in a glove box, and 25 μmol cycloheptatrienyl scandium catalyst h, 10 mL toluene, 2.5 mmol Ali Bu 3 , 5 mmol isoprene and 2.5 mmol [ PhNHMe 2 ][B( C 6 F 5 ) 4 ], reaction time 3 h, reaction temperature 25°C, and other operations were the same as in Example 9 to obtain polyisoprene with a net weight of 0.306 g, a conversion rate of 90%, and a polymerization activity of 4.1 kg·mol -1 · h -1 ; GPC analysis showed that the number average molecular weight of polyisoprene was Mn=18×10 3 , and the molecular weight distribution M w /M n =1.98; the cis 1,4-polymerization selectivity was 89%.
实施例15Example 15
将反应器置于手套箱中,向茄瓶中依次加入25μmol环庚三烯基钪催化剂h,10mL甲苯,2.5mmol AliBu3,5mmol异戊二烯及2.5mmol[PhNHMe2][B(C6F5)4],反应时间3h,反应温度90℃,其余操作同实施例9,得到聚异戊二烯,净重0.34g,转化率100%,聚合活性为4.5kg·mol-1·h-1;GPC分析聚异戊二烯的数均分子量为Mn=12×103,分子量分布Mw/Mn=2.27;顺1,4-聚合选择性76%。The reactor was placed in a glove box, and 25 μmol cycloheptatrienyl scandium catalyst h, 10 mL toluene, 2.5 mmol Ali Bu 3 , 5 mmol isoprene and 2.5 mmol [ PhNHMe 2 ][B( C 6 F 5 ) 4 ], the reaction time was 3 hours, the reaction temperature was 90°C, and the rest of the operations were the same as in Example 9 to obtain polyisoprene with a net weight of 0.34 g, a conversion rate of 100%, and a polymerization activity of 4.5 kg·mol -1 · h -1 ; GPC analysis showed that the number average molecular weight of polyisoprene was Mn=12×10 3 , and the molecular weight distribution M w /M n =2.27; the cis 1,4-polymerization selectivity was 76%.
实施例16Example 16
将反应器置于手套箱中,用20mL干净的小瓶称取2g降冰片烯单体放于50mL茄瓶中,加入4.57mL甲苯,用注射器加入0.5μmol环庚三烯基钪催化剂d,滴加AlMe3甲苯溶液8μL。1h后,拿出手套箱用酸性乙醇(乙醇:浓盐酸=20:1)30mL降解反应液,过滤,并用乙醇洗涤滤出固体;将固体尽量粉碎后,真空烘箱30℃真空干燥,除去溶剂至恒重,得到聚降冰片烯0.04g,产率2.0%,聚合活性为40.0kg·mol-1·h-1;GPC分析聚降冰片烯的数均分子量为Mn=15×103,分子量分布Mw/Mn=1.27。Put the reactor in the glove box, weigh 2g of norbornene monomer into a 50mL eggplant bottle with a 20mL clean vial, add 4.57mL of toluene, add 0.5μmol cycloheptatrienyl scandium catalyst d with a syringe, and drop AlMe 3 toluene solution 8 μL. After 1h, take out the glove box and use 30mL degradation reaction solution with acidic ethanol (ethanol:concentrated hydrochloric acid=20:1), filter, and wash with ethanol to filter out the solid; after the solid is crushed as much as possible, vacuum-dry in a vacuum oven at 30°C, remove the solvent to With constant weight, 0.04 g of polynorbornene was obtained, the yield was 2.0%, and the polymerization activity was 40.0 kg·mol -1 ·h -1 ; the number average molecular weight of polynorbornene by GPC analysis was Mn=15×10 3 , and the molecular weight distribution M w /M n = 1.27.
实施例17Example 17
将反应器置于手套箱中,向茄瓶中依次加入25μmol环庚三烯基钪催化剂d,5mL甲苯,250μmol AliBu3,10mmol苯乙烯及25μmol[Ph3C][B(C6F5)4],反应时间为4h,反应温度25℃。其余操作同实施例9,得到聚苯乙烯;净重0.382g,转化率36.7%,聚合活性为3.82kg·mol-1·h-1;GPC分析聚苯乙烯的数均分子量为Mn=90×103,分子量分布Mw/Mn=1.49。The reactor was placed in a glove box, and 25 μmol cycloheptatrienyl scandium catalyst d, 5 mL toluene, 250 μmol Al i Bu 3 , 10 mmol styrene and 25 μmol [Ph 3 C][B(C 6 F 5 ) 4 ], the reaction time is 4h, and the reaction temperature is 25°C. The remaining operations were the same as in Example 9 to obtain polystyrene; the net weight was 0.382 g, the conversion rate was 36.7%, and the polymerization activity was 3.82 kg·mol −1 ·h −1 ; the number average molecular weight of polystyrene analyzed by GPC was Mn=90×10 3 , molecular weight distribution M w /M n = 1.49.
实施例18Example 18
将反应器置于手套箱中,向茄瓶中依次加入50μmol环庚三烯基钪催化剂d,1mL甲苯,20mol环氧丙烷,密封反应器,转移出手套箱,向反应器中通入CO2,调节压力至6Mpa,然后加热至70℃,反应24h,然后冷却至室温,用氯仿溶解,加入甲醇得到白色固体,用甲醇洗,真空烘干、得到环氧丙烷与CO2的共聚物;产率为43.0%,分子量为Mn=31×103,分子量分布Mw/Mn=1.40。Put the reactor in a glove box, add 50 μmol of cycloheptatrienyl scandium catalyst d, 1 mL of toluene, and 20 mol of propylene oxide to the eggplant bottle in sequence, seal the reactor, transfer it out of the glove box, and inject CO 2 into the reactor , adjusted the pressure to 6Mpa, then heated to 70°C, reacted for 24h, then cooled to room temperature, dissolved in chloroform, added methanol to obtain a white solid, washed with methanol, and dried in vacuum to obtain a copolymer of propylene oxide and CO 2 ; The ratio was 43.0%, the molecular weight was M n =31×10 3 , and the molecular weight distribution M w /M n =1.40.
本发明包括但不限于以上实施例,凡是在本发明精神的原则之下进行的任何等同替换或局部改进,都将视为在本发明的保护范围之内。The present invention includes but is not limited to the above embodiments, and any equivalent replacement or partial improvement under the principle of the spirit of the present invention will be considered within the protection scope of the present invention.
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