CN114308120A - Phosphorus salt amphiphilic bifunctional organic catalyst and preparation method and application thereof - Google Patents
Phosphorus salt amphiphilic bifunctional organic catalyst and preparation method and application thereof Download PDFInfo
- Publication number
- CN114308120A CN114308120A CN202111661001.7A CN202111661001A CN114308120A CN 114308120 A CN114308120 A CN 114308120A CN 202111661001 A CN202111661001 A CN 202111661001A CN 114308120 A CN114308120 A CN 114308120A
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- China
- Prior art keywords
- catalyst
- organic
- amphiphilic
- phosphorus salt
- organic catalyst
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- 239000003054 catalyst Substances 0.000 claims abstract description 78
- -1 polythiocarbonate Polymers 0.000 claims abstract description 44
- 238000002360 preparation method Methods 0.000 claims abstract description 24
- 230000001588 bifunctional effect Effects 0.000 claims abstract description 21
- 150000003017 phosphorus Chemical class 0.000 claims abstract description 19
- 150000003384 small molecules Chemical class 0.000 claims abstract description 9
- 238000005859 coupling reaction Methods 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims abstract description 6
- 238000002156 mixing Methods 0.000 claims abstract description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 24
- 239000000178 monomer Substances 0.000 claims description 19
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 229920000642 polymer Polymers 0.000 claims description 15
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 14
- 125000004122 cyclic group Chemical group 0.000 claims description 14
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 12
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 11
- 238000007151 ring opening polymerisation reaction Methods 0.000 claims description 11
- 239000001569 carbon dioxide Substances 0.000 claims description 10
- UORVGPXVDQYIDP-UHFFFAOYSA-N borane Chemical compound B UORVGPXVDQYIDP-UHFFFAOYSA-N 0.000 claims description 8
- JJWKPURADFRFRB-UHFFFAOYSA-N carbonyl sulfide Chemical compound O=C=S JJWKPURADFRFRB-UHFFFAOYSA-N 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 8
- 125000001424 substituent group Chemical group 0.000 claims description 8
- 239000012372 hydroboration reagent Substances 0.000 claims description 7
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 6
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 6
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 6
- 229910000085 borane Inorganic materials 0.000 claims description 6
- 239000012986 chain transfer agent Substances 0.000 claims description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 5
- 125000005842 heteroatom Chemical group 0.000 claims description 5
- 239000003960 organic solvent Substances 0.000 claims description 5
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- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 4
- 230000009471 action Effects 0.000 claims description 4
- 125000001931 aliphatic group Chemical group 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000003277 amino group Chemical group 0.000 claims description 4
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 4
- 229910052698 phosphorus Inorganic materials 0.000 claims description 4
- 229910052710 silicon Inorganic materials 0.000 claims description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 claims description 4
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- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 3
- 230000001476 alcoholic effect Effects 0.000 claims description 3
- 125000003342 alkenyl group Chemical group 0.000 claims description 3
- 125000000304 alkynyl group Chemical group 0.000 claims description 3
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- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 3
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 125000000524 functional group Chemical group 0.000 claims description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 3
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 2
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 claims description 2
- 125000002843 carboxylic acid group Chemical group 0.000 claims description 2
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 2
- 238000006197 hydroboration reaction Methods 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- 239000012948 isocyanate Substances 0.000 claims description 2
- 150000002513 isocyanates Chemical class 0.000 claims description 2
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- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
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- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- 150000004714 phosphonium salts Chemical class 0.000 claims 2
- LWNGJAHMBMVCJR-UHFFFAOYSA-N (2,3,4,5,6-pentafluorophenoxy)boronic acid Chemical compound OB(O)OC1=C(F)C(F)=C(F)C(F)=C1F LWNGJAHMBMVCJR-UHFFFAOYSA-N 0.000 claims 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical group [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims 1
- 229910002651 NO3 Inorganic materials 0.000 claims 1
- 229910019142 PO4 Inorganic materials 0.000 claims 1
- 150000004703 alkoxides Chemical class 0.000 claims 1
- 150000001540 azides Chemical class 0.000 claims 1
- 229910052796 boron Inorganic materials 0.000 claims 1
- 150000007942 carboxylates Chemical class 0.000 claims 1
- 229910052744 lithium Inorganic materials 0.000 claims 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-M phenolate Chemical compound [O-]C1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-M 0.000 claims 1
- 239000010452 phosphate Substances 0.000 claims 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 18
- 238000006116 polymerization reaction Methods 0.000 abstract description 15
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Abstract
Description
技术领域technical field
本发明涉及一种磷盐两亲性双功能化有机催化剂及其制备方法和应用,属于有机催化剂合成及应用领域。The invention relates to a phosphorus salt amphiphilic bifunctional organic catalyst, a preparation method and application thereof, and belongs to the field of organic catalyst synthesis and application.
背景技术Background technique
有机催化剂因其廉价易得、低生物毒性等引起了科研工作者的关注,但相比较于有机催化剂在有机方法学中的应用,有机催化剂在高分子合成制备领域中仍然处于萌芽期,目前制备的高分子材料包括:聚酯、聚碳酸酯、聚醚、聚酰胺、聚硅氧烷、聚氨酯等。Organocatalysts have attracted the attention of scientific researchers because of their cheapness, easy availability and low biological toxicity. However, compared with the application of organic catalysts in organic methodology, organic catalysts are still in their infancy in the field of polymer synthesis and preparation. The polymer materials include: polyester, polycarbonate, polyether, polyamide, polysiloxane, polyurethane, etc.
目前常用的有机催化体系主要包含以下几类:羧酸类催化体系、吡啶碱类催化体系、氮杂环卡宾类催化体系、含氮有机碱(胍基、脒基、胺类)催化体系、硫脲/脲+胺或硫脲/脲+碱(有机强碱或其它碱)、磷腈碱类催化体系等,这些催化体系已被用于环氧烷烃与二氧化碳制备聚碳酸酯,环氧烷烃与环氧酸酐制备聚酯,环氧烷烃开环聚合制备聚醚,环内酯开环聚合制备聚酯高分子材料,环状碳酸酯开环制备聚碳酸酯,内酰胺开环聚合得到聚酰胺,环状硅氧烷开环聚合制备聚硅氧烷,催化(甲基)丙烯酸酯聚合得到聚(甲基)丙烯酸酯,催化乙烯基醚聚合得到官能化聚乙烯。At present, the commonly used organic catalytic systems mainly include the following categories: carboxylic acid catalytic systems, pyridine base catalytic systems, nitrogen heterocyclic carbene catalytic systems, nitrogen-containing organic bases (guanidine, amidine, amine) catalytic systems, sulfur Urea/urea+amine or thiourea/urea+base (strong organic base or other base), phosphazene base catalytic system, etc., these catalytic systems have been used in the preparation of polycarbonate from alkylene oxide and carbon dioxide, alkylene oxide and carbon dioxide. Polyester is prepared by epoxy anhydride, polyether is prepared by ring-opening polymerization of alkylene oxide, polyester polymer material is prepared by ring-opening polymerization of cyclic lactone, polycarbonate is prepared by ring-opening of cyclic carbonate, and polyamide is obtained by ring-opening polymerization of lactam. The ring-opening polymerization of cyclic siloxane is used to prepare polysiloxane, the polymerization of (meth)acrylate is catalyzed to obtain poly(meth)acrylate, and the polymerization of vinyl ether is catalyzed to obtain functionalized polyethylene.
上述聚合反应机理主要包括:亲电活化单体机理、亲核活化单体、引发剂的亲核活化、单体和引发剂协同活化等聚合机理。硫脲/脲+有机碱、磷腈碱、卡宾、含氮有机碱已被文献报道作为环内酯、环氧烷烃、环氧硅烷、环状碳酸酯等单体的开环聚合中,通过活化引发剂得到活性种引发聚合反应,实现链增长。The above-mentioned polymerization mechanism mainly includes: electrophilic activation of monomer mechanism, nucleophilic activation of monomer, nucleophilic activation of initiator, and synergistic activation of monomer and initiator. Thiourea/urea + organic bases, phosphazene bases, carbene, nitrogen-containing organic bases have been reported in the literature as cyclic lactones, alkylene oxides, epoxy silanes, cyclic carbonates and other monomers in the ring-opening polymerization. The initiator obtains active species to initiate the polymerization reaction and realize chain growth.
鎓盐可以与路易斯酸三烷基硼构建酸碱对或磷腈/醇/三烷基硼构建多组分催化体系用于聚合反应中。三烷基硼作为路易斯酸和亲电试剂,可以活化单体稳定聚合物活性种链末端,鎓盐、磷腈/醇具有亲核性作为引发剂,这种双组分或多组分的体系可以有效提高聚合反应的活性和可控性。如文献中报道的三乙基硼和磷腈类化合物用于环氧烷烃的开环聚合,二氧化碳和环氧烷烃共聚合制备聚碳酸酯,环氧烷烃和杂原子联烯共聚制备聚碳酸酯,环氧和酸酐共聚制备聚酯等。Onium salts can be used with Lewis acid trialkylboron to construct acid-base pair or phosphazene/alcohol/trialkylboron to construct multi-component catalytic system for polymerization. As Lewis acid and electrophilic reagent, trialkylboron can activate monomers to stabilize polymer active species chain ends. Onium salts and phosphazenes/alcohols have nucleophilic properties as initiators. This two-component or multi-component system can Effectively improve the activity and controllability of the polymerization reaction. As reported in the literature, triethylboron and phosphazene compounds are used for the ring-opening polymerization of alkylene oxide, the copolymerization of carbon dioxide and alkylene oxide to prepare polycarbonate, and the copolymerization of alkylene oxide and heteroatom allene to prepare polycarbonate, Epoxy and acid anhydride copolymerization to prepare polyester, etc.
但是现有有机催化体系的特点在于亲核、亲电试剂两组分或多组分混合甚至加入助催化剂或者引发剂才能实现聚合反应,给聚合反应的试剂操作,精确性及机理性研究带来了困难;多组分的称量和量取加大了实验操作的误差。However, the characteristics of the existing organic catalytic systems are that two or more components of nucleophilic and electrophilic reagents can be mixed or even added with co-catalysts or initiators to realize the polymerization reaction, which brings great advantages to the reagent operation, accuracy and mechanism research of the polymerization reaction. The difficulty is increased; the weighing and measuring of multiple components increases the error of the experimental operation.
发明内容SUMMARY OF THE INVENTION
本发明为了解决上述现有技术存在的问题,提供一种磷盐两亲性双功能化有机催化剂及其制备方法和应用。In order to solve the above-mentioned problems in the prior art, the present invention provides a phosphorus salt amphiphilic bifunctional organic catalyst and its preparation method and application.
本发明的技术方案:Technical scheme of the present invention:
一种磷盐两亲性双功能化有机催化剂,结构式如下:A phosphorus salt amphiphilic bifunctional organic catalyst, the structural formula is as follows:
式中X为负离子,R1和R2为相同或不同的取代基,或者R1和R2通过共价键成键或者成环,n为1以上的整数;Y为其中R1、R2和R3分别为氢原子或者取代/未取代/含有N、O、P、Si、S原子中一种或两种以上的C1-C50的烷基、C3-C50的环烷基、C3-C50的烯基、C3-C50的炔基、C6-C50的芳基、C3-C50的杂环基、C5-C50的杂或全碳芳香基中的一种或两种以上的组合。In the formula, X is a negative ion, R 1 and R 2 are the same or different substituents, or R 1 and R 2 form a bond or ring through a covalent bond, and n is an integer of 1 or more; Y is wherein R 1 , R 2 and R 3 are respectively a hydrogen atom or a substituted/unsubstituted/containing one or more of N, O, P, Si, and S atoms of a C1-C50 alkyl group, a C3-C50 ring One or more of alkyl group, C3-C50 alkenyl group, C3-C50 alkynyl group, C6-C50 aryl group, C3-C50 heterocyclic group, C5-C50 hetero or full carbon aryl group The combination.
进一步限定,Y为BR3,有机催化剂为如下的结构:Further limit, Y is BR3, the organic catalyst is the following structure:
n为1以上的整数,且链的种类不仅限于碳链,也可以为其它包含杂原子,如Si,N,O,P,S的杂原子碳链;BR3为环状的硼烷或者脂肪族或者芳香族的硼烷,R3的结构如下:n is an integer of 1 or more, and the type of chain is not limited to carbon chains, but can also be other heteroatom carbon chains containing heteroatoms, such as Si, N, O, P, S; BR 3 is cyclic borane or aliphatic aromatic or aromatic borane, the structure of R 3 is as follows:
其中为连接键,m为1-30的整数。in is the connection bond, m is an integer from 1 to 30.
进一步限定,X为氟离子、氯离子、溴离子、碘离子、氢氧根离子、硝酸根离子、叠氮根离子、四氟硼酸阴离子、四(五氟苯基)硼酸锂阴离子、四羰基镍阴离子、碳酸根离子、磺酸根离子、磷酸根离子、次氯酸根离子、羧酸根离子、烷氧根离子、酚氧根离子中的一种两种以上的组合。Further limited, X is fluoride ion, chloride ion, bromide ion, iodide ion, hydroxide ion, nitrate ion, azide ion, tetrafluoroborate anion, lithium tetrakis(pentafluorophenyl)borate anion, nickel tetracarbonyl A combination of two or more of anions, carbonate ions, sulfonate ions, phosphate ions, hypochlorite ions, carboxylate ions, alkoxy ions, and phenoxy ions.
更进一步限定,有机催化剂为如下结构:Further limited, the organic catalyst is the following structure:
更进一步限定,膦上的取代基不仅限于苯环,还可以是苯环1取代,2取代,3取代,4取代,5取代或者多元环桥联的取代基。For further limitation, the substituent on the phosphine is not limited to the benzene ring, but can also be a 1-substituted, 2-substituted, 3-substituted, 4-substituted, 5-substituted or multi-ring bridged substituent on the benzene ring.
更进一步限定,PhO-可以是单取代苯酚或者多取代苯酚。To further define, PhO- can be a mono-substituted phenol or a poly-substituted phenol.
更进一步限定,碳链的长度不仅限于3,也可以大于3的整数的碳链。For further limitation, the length of the carbon chain is not limited to 3, but can also be a carbon chain that is an integer greater than 3.
进一步限定,有机催化剂为如下结构:Further limited, the organic catalyst is the following structure:
更进一步限定,膦上的取代基不仅限于甲基,还可以是乙基、丙基、丁基,异丁基,戊基,环戊基,己基,环己基,辛基,环辛基,或其甲基1取代,2取代,3取代,4取代,5取代或者其它多环烷基及取代的多环烷基取代基。Further limited, the substituent on the phosphine is not limited to methyl, but can also be ethyl, propyl, butyl, isobutyl, pentyl, cyclopentyl, hexyl, cyclohexyl, octyl, cyclooctyl, or Its methyl group is 1-substituted, 2-substituted, 3-substituted, 4-substituted, 5-substituted or other polycycloalkyl and substituted polycycloalkyl substituents.
更进一步限定,PhO-可以是单取代苯酚或者多取代苯酚。To further define, PhO- can be a mono-substituted phenol or a poly-substituted phenol.
更进一步限定,碳链的长度不仅限于3,也可以大于3的整数的碳链。For further limitation, the length of the carbon chain is not limited to 3, but can also be a carbon chain that is an integer greater than 3.
上述磷盐两亲性双功能化由含有两个不饱和双键的SM与至少含有一个硼氢键的硼氢化试剂进行硼氢化反应制备获得。The above-mentioned amphiphilic bifunctionalization of phosphorus salts is prepared by the hydroboration reaction of SM containing two unsaturated double bonds and a hydroboration reagent containing at least one boron-hydrogen bond.
进一步限定,有机催化剂的制备方法为:将SM和硼氢化试剂在惰性气氛下混合,加入有机溶剂,在-78~100℃下搅拌1~144h,反应结束后去除有机物和杂质,得的磷盐两亲性双功能化有机催化剂。Further limited, the preparation method of the organic catalyst is as follows: mixing SM and borohydride reagent in an inert atmosphere, adding an organic solvent, stirring at -78-100 ° C for 1-144 h, removing organic matter and impurities after the reaction, and obtaining the phosphorus salt Amphiphilic bifunctional organocatalysts.
进一步限定,SM中季磷盐与硼氢化试剂的摩尔比1:(2~3)。To further limit, the molar ratio of quaternary phosphorus salt and hydroboration reagent in SM is 1:(2-3).
更进一步限定,SM的结构如下:To further define, the structure of SM is as follows:
其中X为负离子,R1和R2为相同或不同的取代基,或者R1和R2通过共价键成键或者成环。Wherein X is a negative ion, R 1 and R 2 are the same or different substituents, or R 1 and R 2 form a bond or a ring through a covalent bond.
更进一步限定,n为1以上的整数,且链的种类不仅限于碳链,也可以为其它包含杂原子,如Si,N,O,P,S的杂原子碳链。To be further limited, n is an integer of 1 or more, and the type of chain is not limited to carbon chains, but can also be other heteroatom carbon chains containing heteroatoms, such as Si, N, O, P, S.
更进一步限定,R1、R2和R3分别为氢原子或者取代/未取代/含有N、O、P、Si、S原子中一种或两种以上的C1-C50的烷基、C3-C50的环烷基、C3-C50的烯基、C3-C50的炔基、C6-C50的芳基、C3-C50的杂环基、C5-C50的杂或全碳芳香基中的一种或两种以上的组合。Further limited, R 1 , R 2 and R 3 are respectively hydrogen atoms or substituted/unsubstituted/containing one or more C1-C50 alkyl groups, C3- One of C50 cycloalkyl group, C3-C50 alkenyl group, C3-C50 alkynyl group, C6-C50 aryl group, C3-C50 heterocyclic group, C5-C50 hetero or full carbon aryl group or combination of two or more.
更进一步限定,X为氟离子、氯离子、溴离子、碘离子、氢氧根离子、硝酸根离子、叠氮根离子、四氟硼酸阴离子、四(五氟苯基)硼酸锂阴离子、四羰基镍阴离子、碳酸根离子、磺酸根离子、磷酸根离子、次氯酸根离子、羧酸根离子、烷氧根离子、酚氧根离子中的一种两种以上的组合。Further limited, X is fluoride ion, chloride ion, bromide ion, iodide ion, hydroxide ion, nitrate ion, azide ion, tetrafluoroborate anion, tetrakis (pentafluorophenyl) lithium borate anion, tetracarbonyl A combination of two or more of nickel anions, carbonate ions, sulfonate ions, phosphate ions, hypochlorite ions, carboxylate ions, alkoxy ions, and phenoxy ions.
更进一步限定,硼氢化试剂为含有如下结构中一种或两种以上组合的环状、脂肪族或芳香族的硼烷:Further limited, the hydroboration reagent is a cyclic, aliphatic or aromatic borane containing one or more of the following structures:
其中为连接键,m为1-30的整数。in is the connection bond, m is an integer from 1 to 30.
更进一步限定,硼氢化试剂为9-硼双环(3,3,1)-壬烷。More specifically, the hydroboration reagent is 9-borabicyclo(3,3,1)-nonane.
更进一步限定,有机溶剂为四氢呋喃、苯、甲苯、氯仿、二氯甲烷、己烷、乙醚、四氯化碳、N,N-二甲基甲酰胺、乙酸乙酯、1,4-二氧六环的一种或两种以上以任意比例混合。Further limited, the organic solvent is tetrahydrofuran, benzene, toluene, chloroform, dichloromethane, hexane, ether, carbon tetrachloride, N,N-dimethylformamide, ethyl acetate, 1,4-dioxane One kind or two or more kinds of rings are mixed in any ratio.
上述磷盐两亲性双功能化有机催化剂在制备有机小分子或者高分子材料中的应用,其中有机小分子或者高分子材料由一种或两种以上环状单体在催化剂的作用下开环聚合反应得到,或者由环状单体与二氧化碳、二硫化碳、硫氧化碳、异硫氰酯、异氰酸酯或一氧化碳在催化剂的作用下耦合得到。Application of the above-mentioned phosphorus salt amphiphilic bifunctional organic catalyst in the preparation of organic small molecules or polymer materials, wherein the organic small molecules or polymer materials are ring-opened by one or more cyclic monomers under the action of catalysts It is obtained by a polymerization reaction, or is obtained by coupling a cyclic monomer with carbon dioxide, carbon disulfide, carbon sulfide, isothiocyanate, isocyanate or carbon monoxide under the action of a catalyst.
进一步限定,具体的应用方法为:将催化剂与环状单体按照摩尔比为1:(200~10000)的配比混合,在-40~25℃条件下,反应0.16~6h,所得聚合物的分子量在1~4640kg/mol的范围内,分子量分布在1.02~1.3的范围内。Further limited, the specific application method is as follows: the catalyst and the cyclic monomer are mixed in a molar ratio of 1:(200-10000), and the reaction is carried out at -40-25°C for 0.16-6h. The molecular weight is in the range of 1~4640kg/mol, and the molecular weight distribution in the range of 1.02 to 1.3.
进一步限定,环状单体包含以下结构中一种或种以上组合:Further limited, the cyclic monomer includes one or more combinations of the following structures:
更进一步限定,有机小分子产物为二氧化碳/二硫化碳与环氧烷烃/环硫烷烃经过催化剂催化耦合反应得到环状碳酸酯。In a further limitation, the organic small molecule product is carbon dioxide/carbon disulfide and alkylene oxide/sulfane through the catalytic coupling reaction of catalyst to obtain cyclic carbonate.
更进一步限定,有机小分子产物为CO与环氧烷烃经过催化剂催化耦合反应得到的环内酯。To be further limited, the organic small molecule product is a cyclic lactone obtained by the catalytic coupling reaction of CO and alkylene oxide through a catalyst.
更进一步限定,有机小分子产物为硫氧化碳与环氧烷烃/环硫烷烃经过催化剂催化耦合得到环状硫代碳酸酯。In a further limitation, the organic small molecule product is a cyclic thiocarbonate obtained by catalytic coupling of carbon oxysulfide and alkylene oxide/sulfane through a catalyst.
更进一步限定,聚合物为二氧化碳与环氧烷烃经过催化剂催化共聚得到的脂肪族聚碳酸酯或聚醚。More specifically, the polymer is an aliphatic polycarbonate or polyether obtained by the catalytic copolymerization of carbon dioxide and alkylene oxide through a catalyst.
更进一步限定,聚合物为环氧烷烃经过催化剂催化开环聚合得到的聚醚;环硫醚经过催化剂催化开环聚合得到的聚硫醚;环氧烷烃与环状酸酐经过催化剂催化得到的聚酯;杂原子联烯与杂原子环状化合物共聚得到的聚杂原子碳酸酯经过催化剂催化得到的聚酯;环氧烷烃与一氧化碳经过催化剂催化聚合得到的聚酯。It is further limited that the polymer is a polyether obtained by catalyzing ring-opening polymerization of alkylene oxide; a polysulfide obtained by ring-opening polymerization catalyzed by a cyclic sulfide; a polyester obtained by catalyzing an alkylene oxide and a cyclic acid anhydride through a catalyst ; Polyester obtained by the copolymerization of heteroatom allene and heteroatom cyclic compound through catalyst catalysis; polyester obtained by catalyst catalyzed polymerization of alkylene oxide and carbon monoxide.
更进一步限定,通过调节环氧烷烃、酸酐、环内酯、二氧化碳的加料顺序制备聚醚-聚酯、聚酯-聚碳酸酯、聚醚-聚碳酸酯两嵌段、三嵌段、多嵌段聚合物、梯度或随机共聚物。To be further limited, polyether-polyester, polyester-polycarbonate, polyether-polycarbonate diblock, triblock, multiblock are prepared by adjusting the feeding sequence of alkylene oxide, acid anhydride, cyclic lactone, and carbon dioxide. segmented, gradient or random copolymers.
更进一步限定,有机催化剂CAT1-CAT6和CAT13-CAT18用于催化环氧乙烷(EO),环氧丙烷(PO),环氧丁烷(BO),环氧环己基(CHO),氧化柠檬烯(LO),4-乙烯基环氧环己烯(CVHO)或烯丙基缩水甘油醚(AGE)均聚或者共聚得到聚醚,或者用于催化环氧乙烷(EO),环氧丙烷(PO),环氧丁烷(BO),环氧环己基(CHO),氧化柠檬烯(LO),4-乙烯基环氧环己烯(CVHO)或烯丙基缩水甘油醚(AGE)与CO2共聚得到聚碳酸酯或者环状碳酸酯。Further limited, organic catalysts CAT1-CAT6 and CAT13-CAT18 are used to catalyze ethylene oxide (EO), propylene oxide (PO), butylene oxide (BO), cyclohexyl oxide (CHO), limonene oxide ( LO), 4-vinyl epoxycyclohexene (CVHO) or allyl glycidyl ether (AGE) homopolymerization or copolymerization to obtain polyether, or used to catalyze ethylene oxide (EO), propylene oxide (PO ), butylene oxide (BO), epoxycyclohexyl (CHO), limonene oxide (LO), 4-vinyl epoxycyclohexene (CVHO) or allyl glycidyl ether (AGE) copolymerized with CO2 Polycarbonate or cyclic carbonate.
更进一步限定,有机催化剂CAT1-CAT6和CAT13-CAT18用于催化环氧乙烷(EO),环氧丙烷(PO),环氧丁烷(BO),环氧环己基(CHO),氧化柠檬烯(LO),4-乙烯基环氧环己烯(CVHO)或烯丙基缩水甘油醚(AGE)与环状马来酸酐(MA)、丁二酸酐(SA)、二甘醇酐(DGA)或者邻苯二甲酸酐(PA)共聚得到聚酯。Further limited, organic catalysts CAT1-CAT6 and CAT13-CAT18 are used to catalyze ethylene oxide (EO), propylene oxide (PO), butylene oxide (BO), cyclohexyl oxide (CHO), limonene oxide ( LO), 4-vinyl epoxycyclohexene (CVHO) or allyl glycidyl ether (AGE) with cyclic maleic anhydride (MA), succinic anhydride (SA), diethylene glycol anhydride (DGA) or Polyester is obtained by copolymerization of phthalic anhydride (PA).
更进一步限定,有机催化剂CAT1-CAT2和CAT6用于催化EO,PO,BO或者AGE均聚或者共聚得到聚醚,且聚合反应为活性聚合。More specifically, the organic catalysts CAT1-CAT2 and CAT6 are used to catalyze the homopolymerization or copolymerization of EO, PO, BO or AGE to obtain polyether, and the polymerization reaction is living polymerization.
更进一步限定,有机催化剂CAT1-CAT2和CAT6用于催化丙交酯(LA),β-丁内酯(β-BL),γ-丁内酯(γ-BL),δ-戊内酯(δ-VL)或ε-己内酯(ε-CL)开环聚合或共聚得到聚酯。Further limited, organic catalysts CAT1-CAT2 and CAT6 are used to catalyze lactide (LA), β-butyrolactone (β-BL), γ-butyrolactone (γ-BL), δ-valerolactone (δ -VL) or ε-caprolactone (ε-CL) ring-opening polymerization or copolymerization to obtain polyester.
更进一步限定,有机催化剂CAT1-CAT2和CAT6用于催化环硫乙烷(ES),环硫丙烷(PS),环硫己烷(CHS)与二氧化碳共聚得到聚硫代碳酸酯;或者用于催化2-苯基环硫乙烷(SS)或PS与CO2共聚得到环状硫代碳酸酯。To further limit, the organic catalysts CAT1-CAT2 and CAT6 are used to catalyze the copolymerization of ethylene sulfide (ES), propylene sulfide (PS), and ethylene sulfide (CHS) with carbon dioxide to obtain polythiocarbonate; or used for catalysis 2-Phenyl thioethane (SS) or PS is copolymerized with CO to give cyclic thiocarbonates.
更进一步限定,有机催化剂CAT1-CAT2和CAT6用于催化环氧丙烷(PO)与氧硫化碳共聚得到聚硫代碳酸酯,或者用于催化环硫乙烷(ES)与氧硫化碳或者二硫化碳共聚得到聚硫代碳酸酯,或者用于催化环氧丙烷(PO)与二硫化碳共聚得到聚醚。Further limited, organic catalysts CAT1-CAT2 and CAT6 are used to catalyze the copolymerization of propylene oxide (PO) and carbon oxysulfide to obtain polythiocarbonate, or to catalyze the copolymerization of ethylene sulfide (ES) with carbon oxysulfide or carbon disulfide. Obtain polythiocarbonate, or be used to catalyze the copolymerization of propylene oxide (PO) and carbon disulfide to obtain polyether.
更进一步限定,有机催化剂制备聚合物时,可以在链转移剂存在的条件下进行,因此可以调控制备聚合物的分子量(高低分子量聚合物都可以制备),降低催化剂的用量,降低聚合物的分子量分布,制备带有功能性末端官能团的聚合物(如酯基,酚基,氨基,羟基,叠氮基等)。To further limit, when the organic catalyst prepares the polymer, it can be carried out in the presence of a chain transfer agent, so the molecular weight of the prepared polymer can be regulated (both high and low molecular weight polymers can be prepared), the amount of catalyst is reduced, and the molecular weight of the polymer can be reduced. Distribution, preparation of polymers with functional end functional groups (such as ester groups, phenolic groups, amino groups, hydroxyl groups, azide groups, etc.).
更进一步限定,具体为在聚合反应体系中加入一种或多种醇化合物,酸化合物,胺化合物,多元醇,多元羧酸,多元醇,水作为链转移剂,制备相应的聚合物多元醇或者多远硫醇;或者在聚合反应体系中加入带有醇羟基,酚羟基,氨基,羧基的一种或者多种聚合物作为大分子链转移剂制备相应的嵌段共聚物或者接枝共聚物。It is further limited, specifically adding one or more alcohol compounds, acid compounds, amine compounds, polyols, polycarboxylic acids, polyols, and water as chain transfer agents in the polymerization reaction system to prepare corresponding polymer polyols or Polythiol; or adding one or more polymers with alcoholic hydroxyl groups, phenolic hydroxyl groups, amino groups, and carboxyl groups as macromolecular chain transfer agents in the polymerization reaction system to prepare corresponding block copolymers or graft copolymers.
进一步限定,链转移剂包含以下结构中一种或种以上组合:Further limited, the chain transfer agent comprises one or more combinations of the following structures:
其中代表大分子链转移剂的主链,且主链上所示的醇羟基、酚羟基、氨基或羧酸基不代表官能团的实际个数,实际个数为1以上的任意整数。in represents the backbone of the macromolecular chain transfer agent, and The alcoholic hydroxyl group, phenolic hydroxyl group, amino group or carboxylic acid group shown on the main chain does not represent the actual number of functional groups, and the actual number is any integer of 1 or more.
进一步限定,有机催化剂制备聚合物时,在聚合反应体系中还可以加入路易斯酸,路易斯碱,或者其他多元化催化剂或者助催化剂。To further limit, when the organic catalyst is used to prepare the polymer, Lewis acid, Lewis base, or other diversified catalysts or co-catalysts may also be added to the polymerization reaction system.
上述磷盐两亲性双功能化有机催化剂负载在无机或有机物质上用于制备有机小分子或者高分子材料,更有有利于催化剂的可循环使用,避免催化剂最大程度的流失。The above-mentioned phosphorus salt amphiphilic bifunctional organic catalyst is supported on inorganic or organic substances for preparing organic small molecules or polymer materials, which is more conducive to the recyclable use of the catalyst and avoids the loss of the catalyst to the greatest extent.
本发明具有以下有益效果:The present invention has the following beneficial effects:
(1)本发明提供的磷盐双亲性双功能的有机催化剂将亲核亲电基团以及引发物种糅合于一个催化体系,具有亲核和亲电双功能位点,避免了使用复杂多组分多元催化体系。(1) The phosphorous salt amphiphilic bifunctional organic catalyst provided by the present invention combines nucleophilic and electrophilic groups and initiating species into one catalytic system, has nucleophilic and electrophilic bifunctional sites, and avoids the use of complex multi-component catalytic system.
(2)本发明提供的磷盐双亲性双功能的有机催化剂还具有明确的结构,组分精确,协同催化的特点,这是以往多元化体系很难达到的。(2) The phosphorous salt amphiphilic bifunctional organic catalyst provided by the present invention also has the characteristics of definite structure, precise components and synergistic catalysis, which is difficult to achieve in the past diversified systems.
(3)本发明提供的磷盐双亲性双功能的有机催化剂制备方法具有原料易得、合成路线短和简单等特点。(3) The preparation method of the phosphorus salt amphiphilic bifunctional organic catalyst provided by the present invention has the characteristics of easy availability of raw materials, short and simple synthesis route and the like.
(4)本发明提供的磷盐双亲性双功能的有机催化剂用于聚醚,聚酯,聚碳酸酯,聚硫代碳酸酯,聚硫醚等高分子材料的制备以及其嵌段或者随机共聚物的合成,还可以进行有机小分子偶联反应制备环状碳酸酯,内酯,硫代环状碳酸酯的精细化学品,具有高效、高选择性、可控性等特点。(4) Phosphorus salt amphiphilic bifunctional organic catalyst provided by the present invention is used for the preparation of polymer materials such as polyether, polyester, polycarbonate, polythiocarbonate, polysulfide and the like and the block or random copolymerization thereof It can also carry out organic small molecule coupling reaction to prepare fine chemicals such as cyclic carbonate, lactone and thiocyclic carbonate. It has the characteristics of high efficiency, high selectivity and controllability.
附图说明Description of drawings
图1为CAT1的1H NMR谱图;Figure 1 is the 1 H NMR spectrum of CAT1;
图2为CAT2的1H NMR谱图;Figure 2 is the 1 H NMR spectrum of CAT2;
图3为纯PPO的1H NMR谱图;Figure 3 is the 1 H NMR spectrum of pure PPO;
图4为效果例1的GPC曲线图;Fig. 4 is the GPC curve diagram of effect example 1;
图5为Poly(AGE)的1H NMR谱图;Figure 5 is the 1 H NMR spectrum of Poly(AGE);
图6为Poly(BO)的1H NMR谱图。Figure 6 is a 1 H NMR spectrum of Poly(BO).
具体实施方式Detailed ways
下述实施例中所使用的实验方法如无特殊说明均为常规方法。所用材料、试剂、方法和仪器,未经特殊说明,均为本领域常规材料、试剂、方法和仪器,本领域技术人员均可通过商业渠道获得。The experimental methods used in the following examples are conventional methods unless otherwise specified. The used materials, reagents, methods and instruments, unless otherwise specified, are conventional materials, reagents, methods and instruments in the art, which can be obtained by those skilled in the art through commercial channels.
实施例1Example 1
催化剂CAT1的合成,合成路线如下:The synthesis of catalyst CAT1, the synthetic route is as follows:
其中,的分子结构式如下:in, The molecular structure is as follows:
制备过程如下:The preparation process is as follows:
在火焰干燥的Schlenk容器中,将二烯丙基二苯基溴化膦(173.6mg,0.5mmol,1当量)和9-硼双环[3.3.1]壬烷(9-BBN)(122mg,1.0mmol,2.0当量)溶解在10mL氯仿中。让反应混合物在80℃下搅拌12小时。去除所有挥发物,并用己烷洗涤所得白色固体3次(10mL),以定量产率得到所需产物,产物1H NMR谱图如图1所示(400MHz,CDCl3,298K)。In a flame-dried Schlenk vessel, combine diallyldiphenylphosphine bromide (173.6 mg, 0.5 mmol, 1 equiv) and 9-borabicyclo[3.3.1]nonane (9-BBN) (122 mg, 1.0 mmol, 2.0 equiv) was dissolved in 10 mL of chloroform. The reaction mixture was allowed to stir at 80°C for 12 hours. All volatiles were removed and the resulting white solid was washed three times with hexanes (10 mL) to give the desired product in quantitative yield, the 1H NMR spectrum of the product is shown in Figure 1 (400 MHz, CDCl3 , 298K).
实施例2Example 2
催化剂CAT2的合成,合成路线如下:The synthesis of catalyst CAT2, the synthetic route is as follows:
其中,的分子结构式如下:in, The molecular structure is as follows:
制备过程如下:The preparation process is as follows:
在火焰干燥的Schlenk容器中,将二烯丙基二苯基碘化膦(307mg,0.78mmol,1当量)和9-硼双环[3.3.1]壬烷(9-BBN)(190.4mg,1.56mmol,2当量)溶解在10mL CHCl3中。让反应混合物在80℃下搅拌12小时。去除所有挥发物,并用己烷洗涤所得白色固体3次(10mL),以定量产率得到所需产物,产物1H NMR谱图如图2所示(400MHz,CDCl3,298K)。In a flame-dried Schlenk vessel, combine diallyldiphenylphosphine iodide (307 mg, 0.78 mmol, 1 equiv) and 9-borabicyclo[3.3.1]nonane (9-BBN) (190.4 mg, 1.56 mmol, 2 equiv) was dissolved in 10 mL of CHCl3 . The reaction mixture was allowed to stir at 80°C for 12 hours. All volatiles were removed and the resulting white solid was washed three times with hexanes (10 mL) to give the desired product in quantitative yield, the 1H NMR spectrum of the product is shown in Figure 2 (400 MHz, CDCl3 , 298K).
实施例3Example 3
催化剂CAT4的合成,合成路线如下:The synthesis of catalyst CAT4, the synthetic route is as follows:
制备过程如下:The preparation process is as follows:
在火焰干燥的Schlenk容器中,将CAT1(118.3mg,0.2mmol,1当量)和苯甲酸钠(115.3mg,0.8mmol,4当量)溶解在8ml的CHCl3中。让反应混合物在室温下搅拌48小时。在氮气氛围下过滤收集滤液,去除所有挥发物,并用己烷洗涤生成的白油3次(10mL),以获得所需的白色定量产物。In a flame dried Schlenk vessel, CAT1 (118.3 mg, 0.2 mmol, 1 equiv) and sodium benzoate (115.3 mg, 0.8 mmol, 4 equiv) were dissolved in 8 ml of CHCl3 . The reaction mixture was allowed to stir at room temperature for 48 hours. The filtrate was collected by filtration under nitrogen to remove all volatiles, and the resulting white oil was washed three times (10 mL) with hexanes to obtain the desired white quantitative product.
实施例4Example 4
催化剂CAT5的合成,合成路线如下:The synthesis of catalyst CAT5, the synthetic route is as follows:
制备过程如下:The preparation process is as follows:
在火焰干燥的Schlenk容器中,将CAT1(118.3mg,0.2mmol,1当量)和乙酸钠(65.6mg,0.8mmol,4当量)溶解在8ml的氯仿中。让反应混合物在室温下搅拌48小时。在氮气氛围下过滤收集滤液,去除所有挥发物,并用己烷洗涤生成的白油3次(10mL),以获得所需的白色定量产物。In a flame dried Schlenk vessel, CAT1 (118.3 mg, 0.2 mmol, 1 equiv) and sodium acetate (65.6 mg, 0.8 mmol, 4 equiv) were dissolved in 8 ml of chloroform. The reaction mixture was allowed to stir at room temperature for 48 hours. The filtrate was collected by filtration under nitrogen to remove all volatiles, and the resulting white oil was washed three times (10 mL) with hexanes to obtain the desired white quantitative product.
实施例5Example 5
催化剂CAT6的合成,合成路线如下:The synthesis of catalyst CAT6, the synthetic route is as follows:
制备过程如下:The preparation process is as follows:
在火焰干燥的Schlenk容器中,将CAT1(118.3mg,0.2mmol,1当量)和三氟乙酸钠(108.8mg,0.8mmol,4当量)溶解在8ml的氯仿中。让反应混合物在室温下搅拌48小时。在氮气氛围下过滤收集滤液,去除所有挥发物,并用己烷洗涤生成的白油3次(10mL),以获得所需的白色定量产物。In a flame dried Schlenk vessel, CAT1 (118.3 mg, 0.2 mmol, 1 equiv) and sodium trifluoroacetate (108.8 mg, 0.8 mmol, 4 equiv) were dissolved in 8 ml of chloroform. The reaction mixture was allowed to stir at room temperature for 48 hours. The filtrate was collected by filtration under nitrogen to remove all volatiles, and the resulting white oil was washed three times (10 mL) with hexanes to obtain the desired white quantitative product.
效果例1Effect example 1
利用催化剂CAT1-CAT6催化环氧丙烷的均聚反应,合成路线如下:Utilize catalyst CAT1-CAT6 to catalyze the homopolymerization of propylene oxide, and the synthetic route is as follows:
制备过程如下:The preparation process is as follows:
在手套箱中,将PO和催化剂,称量到装有磁力搅拌器的提前火焰干燥的5mL耐压瓶小瓶中,将小瓶密封拿出,设定-20~25℃作为反应温度,PO与催化剂摩尔比例为200:1~10000:1,反应时间控制在10~120min。应用例1~12的关键数据整理于表1。In the glove box, weigh PO and catalyst into a 5mL pressure-resistant vial with a magnetic stirrer that was pre-flame-dried, seal the vial out, set -20 to 25°C as the reaction temperature, PO and catalyst The molar ratio is 200:1~10000:1, and the reaction time is controlled at 10~120min. The key data of application examples 1 to 12 are arranged in Table 1.
效果例2Effect example 2
利用催化剂CAT1-CAT6催化环氧烷烃与CO2共聚反应,合成路线如下:Utilize catalyst CAT1-CAT6 to catalyze the copolymerization reaction of alkylene oxide and CO2 , the synthetic route is as follows:
制备过程如下:The preparation process is as follows:
在手套箱中,将环氧烷烃和催化剂加入到反应釜中,将反应釜冲入一定压力的二氧化碳,并在设定的温度条件下进行反应,通过核磁表征单体转化率和产物的选择性(聚碳酸酯,聚醚,环状碳酸酯的比例)。应用例13~36的关键数据整理于表2-5。In the glove box, add the alkylene oxide and the catalyst into the reaction kettle, flush the reaction kettle into a certain pressure of carbon dioxide, and carry out the reaction under the set temperature conditions, and characterize the monomer conversion rate and product selectivity by NMR (Proportion of polycarbonate, polyether, cyclic carbonate). The key data of application examples 13 to 36 are arranged in Table 2-5.
表2Table 2
表3table 3
表4Table 4
表5table 5
效果例3Effect example 3
利用催化剂CAT1-CAT6催化环氧烷烃与环状酸酐共聚,合成路线如下:Utilize catalyst CAT1-CAT6 to catalyze the copolymerization of alkylene oxide and cyclic acid anhydride, and the synthetic route is as follows:
制备过程如下:The preparation process is as follows:
在手套箱里,取适量的环状酸酐,环氧烷烃和催化剂置于耐压瓶中,并在60-180℃条件下反应10min-12h。取反应液测试核磁表征单体转化率及产物的选择性。从甲醇中沉淀出来,过滤干燥后,对聚合物的GPC数据进行分析。应用例37~53的关键数据整理于表6-7。In the glove box, take an appropriate amount of cyclic acid anhydride, alkylene oxide and catalyst into a pressure-resistant bottle, and react at 60-180°C for 10min-12h. The reaction solution was taken and tested by NMR to characterize the conversion rate of monomers and the selectivity of products. After precipitation from methanol and filter drying, the polymer was analyzed for GPC data. The key data of application examples 37 to 53 are arranged in Table 6-7.
表6Table 6
表7Table 7
效果例4Effect example 4
利用催化剂CAT1-CAT6催化环状内酯均聚,合成路线如下:Utilize catalyst CAT1-CAT6 to catalyze cyclic lactone homopolymerization, and the synthetic route is as follows:
制备过程如下:The preparation process is as follows:
在手套箱中,将适量的环状内酯单体和催化剂加入到耐压瓶中,并加入一定量的有机溶剂,在-10℃-80℃条件下反应2-12h。取反应液,测试核磁表征单体的转化率及产物的选择性,过滤聚合物,干燥后得到聚酯目标产物,对其进行GPC测试分析。应用例54~55的关键数据整理于表8。In the glove box, add an appropriate amount of cyclic lactone monomer and catalyst into a pressure-resistant bottle, and add a certain amount of organic solvent, and react at -10℃-80℃ for 2-12h. The reaction solution was taken, the conversion rate of the monomer and the selectivity of the product were characterized by nuclear magnetic resonance, the polymer was filtered, and the polyester target product was obtained after drying, which was subjected to GPC analysis. The key data of Application Examples 54 to 55 are summarized in Table 8.
表8Table 8
效果例5Effect example 5
利用催化剂CAT7-CAT24催化环状内酯均聚,合成路线如下:Utilize catalyst CAT7-CAT24 to catalyze cyclic lactone homopolymerization, and the synthetic route is as follows:
催化剂CAT7-CAT24的制备方法与CAT1-CAT6相同。The preparation method of catalysts CAT7-CAT24 is the same as that of CAT1-CAT6.
制备过程如下:The preparation process is as follows:
在手套箱中,将适量的环氧丙烷单体和催化剂加入到耐压瓶中,在25℃-100℃条件下反应2-12h。取反应液,测试核磁表征单体的转化率及产物的选择性。应用例56~61的关键数据整理于表9。In a glove box, add an appropriate amount of propylene oxide monomer and catalyst into a pressure-resistant bottle, and react at 25°C-100°C for 2-12 hours. The reaction solution was taken and tested by NMR to characterize the conversion rate of monomers and the selectivity of products. The key data of application examples 56 to 61 are summarized in Table 9.
表9Table 9
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CN114716660A (en) * | 2022-05-10 | 2022-07-08 | 青岛科技大学 | Method for preparing catalyst and dihydroxy terminated polyether polyol |
CN114716481A (en) * | 2022-05-10 | 2022-07-08 | 青岛科技大学 | Catalyst and preparation method of functionalized polyether polyol |
CN115260241A (en) * | 2022-05-10 | 2022-11-01 | 青岛科技大学 | Organic catalyst and preparation method of polyester polyol and polycarbonate polyol |
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CN114716660A (en) * | 2022-05-10 | 2022-07-08 | 青岛科技大学 | Method for preparing catalyst and dihydroxy terminated polyether polyol |
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CN115260241A (en) * | 2022-05-10 | 2022-11-01 | 青岛科技大学 | Organic catalyst and preparation method of polyester polyol and polycarbonate polyol |
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