CN114230739B - Linear-nonlinear block polymer and preparation method thereof - Google Patents
Linear-nonlinear block polymer and preparation method thereof Download PDFInfo
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- 229920000642 polymer Polymers 0.000 title claims abstract description 76
- 238000002360 preparation method Methods 0.000 title claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 41
- 238000000034 method Methods 0.000 claims abstract description 11
- 239000003999 initiator Substances 0.000 claims description 30
- 238000010560 atom transfer radical polymerization reaction Methods 0.000 claims description 27
- 239000003153 chemical reaction reagent Substances 0.000 claims description 15
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 11
- 239000003054 catalyst Substances 0.000 claims description 11
- 238000006392 deoxygenation reaction Methods 0.000 claims description 11
- 239000003446 ligand Substances 0.000 claims description 11
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims description 9
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical group N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 8
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 claims description 8
- 238000001556 precipitation Methods 0.000 claims description 6
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims description 5
- KWYHDKDOAIKMQN-UHFFFAOYSA-N N,N,N',N'-tetramethylethylenediamine Chemical compound CN(C)CCN(C)C KWYHDKDOAIKMQN-UHFFFAOYSA-N 0.000 claims description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 4
- 229910021589 Copper(I) bromide Inorganic materials 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- 229910052786 argon Inorganic materials 0.000 claims description 4
- 125000004386 diacrylate group Chemical group 0.000 claims description 4
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 4
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- 238000003756 stirring Methods 0.000 claims description 3
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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 230000005587 bubbling Effects 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 238000010791 quenching Methods 0.000 claims description 2
- 101710141544 Allatotropin-related peptide Proteins 0.000 claims 2
- OZAIFHULBGXAKX-VAWYXSNFSA-N AIBN Substances N#CC(C)(C)\N=N\C(C)(C)C#N OZAIFHULBGXAKX-VAWYXSNFSA-N 0.000 claims 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 claims 1
- 239000012299 nitrogen atmosphere Substances 0.000 claims 1
- 150000003462 sulfoxides Chemical class 0.000 claims 1
- 239000000178 monomer Substances 0.000 abstract description 26
- 229920002554 vinyl polymer Polymers 0.000 abstract description 22
- 238000006116 polymerization reaction Methods 0.000 abstract description 19
- 238000003786 synthesis reaction Methods 0.000 abstract description 17
- 230000015572 biosynthetic process Effects 0.000 abstract description 16
- 238000009826 distribution Methods 0.000 abstract description 6
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- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 2
- 238000005227 gel permeation chromatography Methods 0.000 description 18
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 15
- 238000012546 transfer Methods 0.000 description 13
- 238000010526 radical polymerization reaction Methods 0.000 description 9
- 230000002441 reversible effect Effects 0.000 description 7
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 6
- 238000013467 fragmentation Methods 0.000 description 6
- 238000006062 fragmentation reaction Methods 0.000 description 6
- 239000011541 reaction mixture Substances 0.000 description 6
- 229920001427 mPEG Polymers 0.000 description 5
- YOCIJWAHRAJQFT-UHFFFAOYSA-N 2-bromo-2-methylpropanoyl bromide Chemical compound CC(C)(Br)C(Br)=O YOCIJWAHRAJQFT-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
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- 230000008878 coupling Effects 0.000 description 4
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- 238000010586 diagram Methods 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 description 3
- 239000002202 Polyethylene glycol Substances 0.000 description 3
- YOQLRQUGJROXRV-UHFFFAOYSA-N benzenecarbodithioic acid;4-cyanopentanoic acid Chemical compound N#CC(C)CCC(O)=O.SC(=S)C1=CC=CC=C1 YOQLRQUGJROXRV-UHFFFAOYSA-N 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 229920002521 macromolecule Polymers 0.000 description 3
- 229920001223 polyethylene glycol Polymers 0.000 description 3
- 238000012712 reversible addition−fragmentation chain-transfer polymerization Methods 0.000 description 3
- XFCMNSHQOZQILR-UHFFFAOYSA-N 2-[2-(2-methylprop-2-enoyloxy)ethoxy]ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCOC(=O)C(C)=C XFCMNSHQOZQILR-UHFFFAOYSA-N 0.000 description 2
- HCLJOFJIQIJXHS-UHFFFAOYSA-N 2-[2-[2-(2-prop-2-enoyloxyethoxy)ethoxy]ethoxy]ethyl prop-2-enoate Chemical compound C=CC(=O)OCCOCCOCCOCCOC(=O)C=C HCLJOFJIQIJXHS-UHFFFAOYSA-N 0.000 description 2
- AISZNMCRXZWVAT-UHFFFAOYSA-N 2-ethylsulfanylcarbothioylsulfanyl-2-methylpropanenitrile Chemical compound CCSC(=S)SC(C)(C)C#N AISZNMCRXZWVAT-UHFFFAOYSA-N 0.000 description 2
- VHYFNPMBLIVWCW-UHFFFAOYSA-N 4-Dimethylaminopyridine Chemical compound CN(C)C1=CC=NC=C1 VHYFNPMBLIVWCW-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical group C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- 239000012988 Dithioester Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000005481 NMR spectroscopy Methods 0.000 description 2
- 239000012987 RAFT agent Substances 0.000 description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 125000005022 dithioester group Chemical group 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- PBMIETCUUSQZCG-UHFFFAOYSA-N n'-cyclohexylmethanediimine Chemical compound N=C=NC1CCCCC1 PBMIETCUUSQZCG-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 150000003254 radicals Chemical class 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- 239000012989 trithiocarbonate Substances 0.000 description 2
- HIZCIEIDIFGZSS-UHFFFAOYSA-L trithiocarbonate Chemical compound [S-]C([S-])=S HIZCIEIDIFGZSS-UHFFFAOYSA-L 0.000 description 2
- XRUKRHLZDVJJSX-UHFFFAOYSA-N 4-cyanopentanoic acid Chemical compound N#CC(C)CCC(O)=O XRUKRHLZDVJJSX-UHFFFAOYSA-N 0.000 description 1
- JHWGFJBTMHEZME-UHFFFAOYSA-N 4-prop-2-enoyloxybutyl prop-2-enoate Chemical compound C=CC(=O)OCCCCOC(=O)C=C JHWGFJBTMHEZME-UHFFFAOYSA-N 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- KXDHJXZQYSOELW-UHFFFAOYSA-M Carbamate Chemical compound NC([O-])=O KXDHJXZQYSOELW-UHFFFAOYSA-M 0.000 description 1
- 238000006845 Michael addition reaction Methods 0.000 description 1
- DAKWPKUUDNSNPN-UHFFFAOYSA-N Trimethylolpropane triacrylate Chemical compound C=CC(=O)OCC(CC)(COC(=O)C=C)COC(=O)C=C DAKWPKUUDNSNPN-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- DKVNPHBNOWQYFE-UHFFFAOYSA-N carbamodithioic acid Chemical compound NC(S)=S DKVNPHBNOWQYFE-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 125000004119 disulfanediyl group Chemical group *SS* 0.000 description 1
- 239000012990 dithiocarbamate Substances 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- UKODFQOELJFMII-UHFFFAOYSA-N pentamethyldiethylenetriamine Chemical compound CN(C)CCN(C)CCN(C)C UKODFQOELJFMII-UHFFFAOYSA-N 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- ILWRPSCZWQJDMK-UHFFFAOYSA-N triethylazanium;chloride Chemical compound Cl.CCN(CC)CC ILWRPSCZWQJDMK-UHFFFAOYSA-N 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F293/00—Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule
- C08F293/005—Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule using free radical "living" or "controlled" polymerisation, e.g. using a complexing agent
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2438/00—Living radical polymerisation
- C08F2438/03—Use of a di- or tri-thiocarbonylthio compound, e.g. di- or tri-thioester, di- or tri-thiocarbamate, or a xanthate as chain transfer agent, e.g . Reversible Addition Fragmentation chain Transfer [RAFT] or Macromolecular Design via Interchange of Xanthates [MADIX]
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Graft Or Block Polymers (AREA)
Abstract
本发明公开了一种线性‑非线性嵌段聚合物及其制备方法,属于高分子合成领域。本发明公开的一种线性‑非线性嵌段聚合物是由线性聚合物链段和多乙烯基单体聚合的非线性结构构成,是一种全新拓扑结构聚合物。本发明还公开了其制备方法,在多乙烯基单体可控聚合的基础上,在无氧条件下通过使用大分子RAFT试剂调控或者大分子ATRP引发多乙烯基单体聚合一步制备线性‑非线性嵌段聚合物。该方法反应条件相对温和、聚合产物组成、分子量及分子量分布可控、聚合物拓扑结构易于调节,适合于大规模生产和应用,具有重要的应用价值。
The invention discloses a linear-nonlinear block polymer and a preparation method thereof, belonging to the field of polymer synthesis. A linear-nonlinear block polymer disclosed by the invention is composed of a linear polymer chain segment and a non-linear structure polymerized by polyvinyl monomers, and is a new topology polymer. The invention also discloses its preparation method. On the basis of the controllable polymerization of polyvinyl monomers, under anaerobic conditions, one-step preparation of linear-non- Linear block polymers. The method has relatively mild reaction conditions, controllable polymer composition, molecular weight and molecular weight distribution, and easy adjustment of polymer topology, which is suitable for large-scale production and application, and has important application value.
Description
技术领域technical field
本发明属于高分子合成领域,具体涉及一种线性-非线性嵌段聚合物及其制备方法。The invention belongs to the field of polymer synthesis, and in particular relates to a linear-nonlinear block polymer and a preparation method thereof.
背景技术Background technique
可逆加成-断裂链转移自由基聚合(RAFT)与原子转移自由基聚合(ATRP)由于聚合条件较为温和、单体适用范围广、聚合物的组成和结构易于控制等优势而被广泛应用于聚合物的制备。随着对非线型拓扑结构研究与应用的逐步深入,发现非线性拓扑结构高分子表现出与线性拓扑结构明显不同的性能。通过RAFT或者ATRP聚合只含有一个乙烯基官能团的单乙烯基单体往往只能获得线性高分子。通过将RAFT试剂、ATRP引发剂或者自由基引发剂预先修饰到特定拓扑结构的分子上,再通过单乙烯基单体的RAFT或者ATRP聚合,则可制备刷型、星型、超支化、环化等非线性拓扑结构高分子。此外,基于小分子RAFT链转移剂调控或者小分子ATRP引发剂引发多乙烯基单体聚合合成环化及支化聚合物的研究已取得一定进展。Reversible addition-fragmentation chain transfer radical polymerization (RAFT) and atom transfer radical polymerization (ATRP) are widely used in polymerization due to their advantages such as relatively mild polymerization conditions, wide application range of monomers, and easy control of polymer composition and structure. The preparation of things. With the gradual deepening of the research and application of nonlinear topological structures, it is found that nonlinear topological polymers exhibit significantly different properties from linear topological structures. Polymerization of monovinyl monomers containing only one vinyl functional group by RAFT or ATRP often yields only linear polymers. By pre-modifying RAFT reagents, ATRP initiators or free radical initiators on molecules with specific topological structures, and then polymerizing monovinyl monomers through RAFT or ATRP, brush-type, star-type, hyperbranched, and cyclized and other nonlinear topological polymers. In addition, some progress has been made in the synthesis of cyclized and branched polymers based on the regulation of small molecule RAFT chain transfer agents or the polymerization of polyvinyl monomers initiated by small molecule ATRP initiators.
线性-非线性嵌段聚合物由于其独特的类似于蝌蚪状的拓扑结构而展示出完全不同于线性、刷型、星型、超支化、环化等聚合物的性能,如流体力学体积、玻璃化转变温度、界面性能等,因而在生物医学、涂料、工程材料等领域具有巨大的应用潜力。但上述所有方法均无法一步合成线性-非线性拓扑结构高分子。目前,线性-非线性嵌段聚合物的合成主要采用分链段聚合,通过非共价键作用拼接形成。由于非线性结构合成难度大、效率低,同时线性-非线性嵌段聚合物合成需要考虑非线性结构与线性链段的聚合顺序和嵌段结合方式等因素,使线性-非线性嵌段聚合物合成极具挑战性。Linear-nonlinear block polymers exhibit completely different properties from linear, brush, star, hyperbranched, cyclized, etc. polymers due to their unique tadpole-like topology, such as hydrodynamic volume, glass Transition temperature, interface properties, etc., so it has great application potential in the fields of biomedicine, coatings, engineering materials, etc. However, none of the above methods can synthesize linear-nonlinear topological polymers in one step. At present, the synthesis of linear-nonlinear block polymers mainly adopts segmental polymerization and splicing through non-covalent bonds. Due to the difficulty and low efficiency of nonlinear structure synthesis, and the synthesis of linear-nonlinear block polymers needs to consider factors such as the polymerization order of nonlinear structures and linear segments and the block combination mode, making linear-nonlinear block polymers Synthesis is extremely challenging.
发明内容Contents of the invention
为了克服上述现有技术的缺点,本发明的目的在于提供一种线性-非线性嵌段聚合物及其制备方法,以解决目前线性-非线性嵌段聚合物制备方法不足的问题。In order to overcome the above-mentioned shortcomings of the prior art, the object of the present invention is to provide a linear-nonlinear block polymer and its preparation method to solve the problem of insufficient preparation methods of the current linear-nonlinear block polymer.
为了达到上述目的,本发明采用以下技术方案予以实现:In order to achieve the above object, the present invention adopts the following technical solutions to achieve:
本发明公开了一种线性-非线性嵌段聚合物,该线性-非线性嵌段聚合物由线性聚合物链段和多乙烯基单体聚合的非线性结构构成,其结构式如下:The invention discloses a linear-nonlinear block polymer. The linear-nonlinear block polymer is composed of a linear polymer segment and a non-linear structure polymerized by polyvinyl monomers. Its structural formula is as follows:
式中,m=5~20,p=5~100,q=5~100;In the formula, m=5~20, p=5~100, q=5~100;
R1为*Br或 R 1 is *Br or
R2为 R2 is
式中,n=10~200。In the formula, n=10-200.
本发明还公开了上述线性-非线性嵌段聚合物的制备方法,一种制备方法为以大分子RAFT试剂为链转移,通过引发剂引发多乙烯基单体,进行可逆加成-断裂链转移自由基聚合反应;另一种制备方法为以大分子ATRP引发剂引发多乙烯基单体,通过使用配体和催化剂,进行原子转移自由基聚合反应,得到线性-非线性嵌段聚合物。The invention also discloses a preparation method of the above-mentioned linear-nonlinear block polymer. One preparation method is to use a macromolecular RAFT reagent as a chain transfer, trigger a polyvinyl monomer through an initiator, and perform reversible addition-fragmentation chain transfer Free radical polymerization; another preparation method is to use a macromolecular ATRP initiator to initiate polyvinyl monomers, and use ligands and catalysts to carry out atom transfer free radical polymerization to obtain linear-nonlinear block polymers.
优选地,所述多乙烯基单体为二乙烯基苯、二(甲基)丙烯酸酯、三(甲基)丙烯酸酯、双酚A聚氧乙烯醚二丙烯酸酯、1,4-丁二醇二丙烯酸酯、二乙二醇二甲基丙烯酸酯、四甘醇二丙烯酸酯或三羟甲基丙烷三丙烯酸酯。Preferably, the polyvinyl monomer is divinylbenzene, di(meth)acrylate, tri(meth)acrylate, bisphenol A polyoxyethylene ether diacrylate, 1,4-butanediol Diacrylate, diethylene glycol dimethacrylate, tetraethylene glycol diacrylate, or trimethylolpropane triacrylate.
优选地,所述可逆加成-断裂链转移自由基聚合反应,包括以下步骤:Preferably, the reversible addition-fragmentation chain transfer radical polymerization reaction comprises the following steps:
1)将多乙烯基单体、大分子RAFT试剂和引发剂在溶剂中充分溶解,得到反应混合体系;1) Fully dissolving polyvinyl monomers, macromolecular RAFT reagents and initiators in a solvent to obtain a reaction mixture system;
2)反应混合体系进行除氧,除氧结束后进行聚合反应;2) The reaction mixture system is deoxidized, and the polymerization reaction is carried out after the deoxygenation is completed;
3)对产物进行提纯,得到线性-非线性嵌段聚合物。3) Purifying the product to obtain a linear-nonlinear block polymer.
进一步优选地,步骤1)中,所述大分子RAFT试剂的分子量为500-50000Da,由聚乙二醇单甲醚与4-氰基戊酸二硫代苯甲酸、二硫代酯、二硫代氨基甲酸酯、三硫代碳酸酯或黄原酸酯偶合得到。Further preferably, in step 1), the molecular weight of the macromolecular RAFT agent is 500-50000Da, which is composed of polyethylene glycol monomethyl ether and 4-cyanovaleric acid dithiobenzoic acid, dithioester, dithio It can be obtained by coupling carbamate, trithiocarbonate or xanthate.
进一步优选地,步骤1)中,所述多乙烯基单体、大分子RAFT试剂和引发剂的摩尔比为(50~1000):1:(0.1~1);Further preferably, in step 1), the molar ratio of the polyvinyl monomer, the macromolecular RAFT agent and the initiator is (50-1000):1:(0.1-1);
所述引发剂为偶氮二异丁腈、4,4'-偶氮(4-氰基戊酸)或过氧化苯甲酰;溶剂为2-丁酮。The initiator is azobisisobutyronitrile, 4,4'-azo(4-cyanovaleric acid) or benzoyl peroxide; the solvent is 2-butanone.
优选地,所述原子转移自由基聚合反应,包括以下步骤:Preferably, the atom transfer radical polymerization reaction comprises the following steps:
1)将多乙烯基单体、大分子ATRP引发剂、配体和催化剂充分溶解在溶剂中,得到反应混合体系;1) Fully dissolving polyvinyl monomers, macromolecular ATRP initiators, ligands and catalysts in a solvent to obtain a reaction mixture system;
2)反应混合体系进行除氧;除氧结束后进行聚合反应;2) The reaction mixture system is deoxidized; after the deoxygenation is completed, the polymerization reaction is carried out;
3)对产物进行提纯,得到线性-非线性嵌段聚合物。3) Purifying the product to obtain a linear-nonlinear block polymer.
进一步优选地,步骤1)中,所述大分子ATRP引发剂的分子量为500-50000Da,由聚乙二醇单甲醚与卤代烷烃偶合得到。Further preferably, in step 1), the macromolecular ATRP initiator has a molecular weight of 500-50000 Da and is obtained by coupling polyethylene glycol monomethyl ether with halogenated alkanes.
进一步优选地,步骤1)中,所述多乙烯基单体、大分子ATRP引发剂、配体和催化剂的摩尔比为(50~1000):1:(0.5~5):(0.05~0.5);Further preferably, in step 1), the molar ratio of the polyvinyl monomer, macromolecular ATRP initiator, ligand and catalyst is (50-1000): 1: (0.5-5): (0.05-0.5) ;
所述配体为N,N,N',N”,N”-五甲基二乙烯基三胺,催化剂为CuBr2,溶剂为二甲基亚砜。The ligand is N,N,N',N",N"-pentamethyl divinyl triamine, the catalyst is CuBr 2 , and the solvent is dimethyl sulfoxide.
进一步优选地,所述可逆加成-断裂链转移自由基聚合反应、原子转移自由基聚合反应的聚合反应温度为20℃-80℃。Further preferably, the polymerization reaction temperature of the reversible addition-fragmentation chain transfer radical polymerization and atom transfer radical polymerization is 20°C-80°C.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明公开了一种线性-非线性嵌段聚合物,由线性聚合物链段和多乙烯基聚合的非线性结构构成,是一种全新拓扑结构聚合物,聚合物拓扑结构易于调节,所得聚合物含有大量未反应的双键,可通过迈克尔加成、点击化学等多种方法进行修饰改性,可进一步提高聚合物的功能,扩大聚合物的应用领域。The invention discloses a linear-nonlinear block polymer, which is composed of a linear polymer segment and a non-linear structure of polyvinyl polymerization. It is a new topology polymer, and the polymer topology is easy to adjust. The polymer contains a large number of unreacted double bonds, which can be modified by various methods such as Michael addition and click chemistry, which can further improve the function of the polymer and expand the application field of the polymer.
本发明还公开了线性-非线性嵌段聚合物的制备方法,一种制备方法为以大分子RAFT试剂为链转移,通过引发剂引发多乙烯基单体,在无氧条件下进行可逆加成-断裂链转移自由基聚合,另一种制备方法为以大分子ATRP引发剂引发多乙烯基单体,通过使用配体和催化剂,在无氧条件下进行原子转移自由基聚合,得到线性-非线性嵌段聚合物。本发明公开的上述制备方法为线性-非线性拓扑结构聚合物的合成开辟了一条新途径,丰富了拓扑结构聚合物的种类,对拓扑结构聚合物的化学合成具有重要的启示意义;并且反应原料广泛易得、反应条件温和、聚合物的组成、结构、分子量及分子量分布易于调控、产物后处理简单、聚合易于操作,适合大规模生产应用。The invention also discloses a preparation method of a linear-nonlinear block polymer. A preparation method is to use a macromolecular RAFT reagent as a chain transfer, trigger a polyvinyl monomer through an initiator, and perform reversible addition under anaerobic conditions -fragmented chain transfer radical polymerization, another preparation method is to initiate polyvinyl monomers with macromolecular ATRP initiators, and carry out atom transfer radical polymerization under anaerobic conditions by using ligands and catalysts to obtain linear-non- Linear block polymers. The above-mentioned preparation method disclosed by the present invention opens up a new way for the synthesis of linear-nonlinear topological polymers, enriches the types of topological polymers, and has important enlightenment significance for the chemical synthesis of topological polymers; and the reaction raw materials It is widely and easily available, the reaction conditions are mild, the composition, structure, molecular weight and molecular weight distribution of the polymer are easy to control, the post-treatment of the product is simple, and the polymerization is easy to operate, which is suitable for large-scale production applications.
附图说明Description of drawings
图1为本发明的大分子RAFT试剂mPEG-CPABD合成前后GPC谱图;Fig. 1 is the GPC spectrogram before and after synthesis of macromolecule RAFT reagent mPEG-CPABD of the present invention;
图2为本发明的大分子ATRP引发剂mPEG-Br合成前后GPC谱图;Fig. 2 is the GPC spectrogram before and after synthesis of macromolecular ATRP initiator mPEG-Br of the present invention;
图3为本发明实施例1中线性-非线性嵌段聚合物的合成示意图;Fig. 3 is the synthesizing schematic diagram of the linear-nonlinear block polymer in the embodiment 1 of the present invention;
图4为本发明实施例2中线性-非线性嵌段聚合物的合成示意图;Fig. 4 is the synthesizing schematic diagram of the linear-nonlinear block polymer in the embodiment 2 of the present invention;
图5为本发明实施例1中线性-非线性嵌段聚合物的1HNMR谱图;Fig. 5 is the 1 HNMR spectrogram of the linear-nonlinear block polymer in Example 1 of the present invention;
图6为本发明实施例2中线性-非线性嵌段聚合物的1HNMR谱图;Fig. 6 is the 1 HNMR spectrogram of the linear-nonlinear block polymer in Example 2 of the present invention;
图7为本发明实施例1反应过程中线性-非线性嵌段聚合物分子量变化GPC谱图;Fig. 7 is the GPC spectrogram of linear-nonlinear block polymer molecular weight variation during the reaction process of Example 1 of the present invention;
图8为本发明实施例2反应过程中线性-非线性嵌段聚合物分子量变化GPC谱图;Fig. 8 is the GPC spectrogram of the molecular weight change of the linear-nonlinear block polymer in the reaction process of Example 2 of the present invention;
图9为本发明实施例1线性-非线性嵌段聚合物聚合过程动力学拟合曲线。Fig. 9 is a kinetic fitting curve of the polymerization process of the linear-nonlinear block polymer in Example 1 of the present invention.
具体实施方式Detailed ways
为了使本技术领域的人员更好地理解本发明方案,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分的实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都应当属于本发明保护的范围。In order to enable those skilled in the art to better understand the solutions of the present invention, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are only It is an embodiment of a part of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts shall fall within the protection scope of the present invention.
需要说明的是,本发明的说明书和权利要求书及上述附图中的术语“第一”、“第二”等是用于区别类似的对象,而不必用于描述特定的顺序或先后次序。应该理解这样使用的数据在适当情况下可以互换,以便这里描述的本发明的实施例能够以除了在这里图示或描述的那些以外的顺序实施。此外,术语“包括”和“具有”以及他们的任何变形,意图在于覆盖不排他的包含,例如,包含了一系列步骤或单元的过程、方法、系统、产品或设备不必限于清楚地列出的那些步骤或单元,而是可包括没有清楚地列出的或对于这些过程、方法、产品或设备固有的其它步骤或单元。It should be noted that the terms "first" and "second" in the description and claims of the present invention and the above drawings are used to distinguish similar objects, but not necessarily used to describe a specific sequence or sequence. It is to be understood that the data so used are interchangeable under appropriate circumstances such that the embodiments of the invention described herein can be practiced in sequences other than those illustrated or described herein. Furthermore, the terms "comprising" and "having", as well as any variations thereof, are intended to cover a non-exclusive inclusion, for example, a process, method, system, product or device comprising a sequence of steps or elements is not necessarily limited to the expressly listed instead, may include other steps or elements not explicitly listed or inherent to the process, method, product or apparatus.
本发明公开的一种线性-非线性嵌段聚合物是由线性聚合物链段和多乙烯基单体聚合的非线性结构构成,是一种全新拓扑结构聚合物。A linear-nonlinear block polymer disclosed by the invention is composed of a linear polymer chain segment and a non-linear structure polymerized by polyvinyl monomers, and is a new topology polymer.
本发明公开了一种线性-非线性嵌段聚合物的制备方法,一种制备方法为以大分子RAFT试剂为链转移,通过引发剂引发多乙烯基单体,进行可逆加成-断裂链转移自由基聚合反应,另一种制备方法为以大分子ATRP引发剂引发多乙烯基单体,通过使用配体和催化剂,进行原子转移自由基聚合反应,得到线性-非线性嵌段聚合物。The invention discloses a preparation method of a linear-nonlinear block polymer. A preparation method uses a macromolecular RAFT reagent as a chain transfer, triggers a polyvinyl monomer through an initiator, and performs reversible addition-fragmentation chain transfer Free radical polymerization, another preparation method is to use a macromolecular ATRP initiator to initiate a polyvinyl monomer, and use a ligand and a catalyst to carry out atom transfer free radical polymerization to obtain a linear-nonlinear block polymer.
本发明中大分子RAFT试剂的构建步骤如下:The construction steps of macromolecule RAFT reagent in the present invention are as follows:
使用商品化聚乙二醇单甲醚(mPEG)与4-氰基戊酸二硫代苯甲酸(CPADB)、二硫代酯、二硫代氨基甲酸酯、三硫代碳酸酯或黄原酸酯偶合合成大分子RAFT试剂。首先,将mPEG、4-氰基戊酸二硫代苯甲酸(CPADB)和4-(二甲氨基)吡啶(DMAP)溶于二氯甲烷(DCM)中,通入氮气保护,其次,将上述体系置于冰浴环境下,缓慢滴加溶解在DCM中的环己基碳二亚胺(DCC)溶液,滴加结束后转至室温进一步搅拌反应40h。然后,将得到的产物过滤后用乙醚沉淀提纯、透析、冻干,得到大分子RAFT试剂mPEG-CPADB。Use commercially available polyethylene glycol monomethyl ether (mPEG) with 4-cyanopentanoic acid dithiobenzoic acid (CPADB), dithioester, dithiocarbamate, trithiocarbonate, or xanthogen Ester coupling synthesis of macromolecular RAFT reagents. First, dissolve mPEG, 4-cyanopentanoic acid dithiobenzoic acid (CPADB) and 4-(dimethylamino)pyridine (DMAP) in dichloromethane (DCM), pass through nitrogen protection, and secondly, the above The system was placed in an ice-bath environment, and a solution of cyclohexylcarbodiimide (DCC) dissolved in DCM was slowly added dropwise, and after the addition was completed, it was returned to room temperature for further stirring for 40 h. Then, the obtained product was filtered, purified by ether precipitation, dialyzed and freeze-dried to obtain the macromolecular RAFT reagent mPEG-CPADB.
本发明中大分子ATRP引发剂的构建步骤如下:The construction steps of macromolecule ATRP initiator among the present invention are as follows:
使用商品化mPEG与卤代烷烃合成大分子ATRP引发剂。首先,将mPEG、三乙胺(TEA)溶解在DCM中。在冰浴条件下缓慢滴加溶解在DCM中的2-溴异丁酰溴(BIB),并继续在室温下搅拌反应24h。反应结束后,用去离子水洗涤以去除水溶性三乙胺盐酸盐其次,将有机相干燥后浓缩,再于冰乙醚中沉淀两次。最后收集产品,在真空烘箱中干燥,得到大分子ATRP引发剂mPEG-Br。Macromolecular ATRP initiators were synthesized using commercially available mPEG and halogenated alkanes. First, mPEG, triethylamine (TEA) was dissolved in DCM. 2-Bromoisobutyryl bromide (BIB) dissolved in DCM was slowly added dropwise under ice-bath conditions, and the reaction was continued to stir at room temperature for 24h. After the reaction, it was washed with deionized water to remove water-soluble triethylamine hydrochloride. Next, the organic phase was dried, concentrated, and precipitated twice in glacial ether. Finally, the product was collected and dried in a vacuum oven to obtain the macromolecular ATRP initiator mPEG-Br.
本发明中可逆加成-断裂链转移自由基聚合反应,包括以下步骤:In the present invention, the reversible addition-fragmentation chain transfer radical polymerization reaction comprises the following steps:
1)将多乙烯基单体、大分子RAFT试剂和引发剂偶氮二异丁腈(AIBN)在2-丁酮中充分溶解,得到反应混合体系;多乙烯基单体、大分子RAFT试剂和引发剂的摩尔比为(50~1000):1:(0.1~1);1) Polyvinyl monomers, macromolecular RAFT reagents and initiator azobisisobutyronitrile (AIBN) are fully dissolved in 2-butanone to obtain a reaction mixed system; polyvinyl monomers, macromolecular RAFT reagents and The molar ratio of the initiator is (50-1000): 1: (0.1-1);
2)反应混合体系采用惰性气体置换进行充分除氧,除氧结束后在40~80℃进行聚合反应;2) The reaction mixture system is fully deoxygenated by inert gas replacement, and the polymerization reaction is carried out at 40-80°C after deoxygenation;
3)使用凝胶渗透色谱(GPC)监测聚合物分子量,当分子量达到1000-50000Da时停止反应;3) Use gel permeation chromatography (GPC) to monitor the molecular weight of the polymer, and stop the reaction when the molecular weight reaches 1000-50000Da;
4)采用沉淀法对产物进行提纯,得到分子量在1000-50000Da的线性-非线性嵌段聚合物;4) The product is purified by a precipitation method to obtain a linear-nonlinear block polymer with a molecular weight of 1000-50000Da;
5)通过核磁共振氢谱(1HNMR)与凝胶渗透色谱(GPC)确定聚合物的组成、结构、分子量和分子量分布。5) Determine the composition, structure, molecular weight and molecular weight distribution of the polymer by hydrogen nuclear magnetic resonance spectroscopy ( 1 HNMR) and gel permeation chromatography (GPC).
本发明中原子转移自由基聚合反应,包括以下步骤:Atom transfer radical polymerization among the present invention, comprises the following steps:
1)将多乙烯基单体、大分子ATRP引发剂、配体N,N,N',N”,N”-五甲基二乙烯基三胺和催化剂CuBr2充分溶解在二甲基亚砜(DMSO)中,得到反应混合体系;多乙烯基单体、大分子ATRP引发剂、配体和催化剂的摩尔比为(50~1000):1:(0.5~5):(0.05~0.5);1) Fully dissolve polyvinyl monomer, macromolecular ATRP initiator, ligand N,N,N',N",N"-pentamethyldivinyltriamine and catalyst CuBr 2 in dimethyl sulfoxide (DMSO) to obtain a reaction mixed system; the molar ratio of polyvinyl monomer, macromolecular ATRP initiator, ligand and catalyst is (50-1000): 1: (0.5-5): (0.05-0.5);
2)反应混合体系采用惰性气体置换进行充分除氧,除氧结束后在20~40℃进行聚合反应;2) The reaction mixture system is fully deoxygenated by inert gas replacement, and the polymerization reaction is carried out at 20-40°C after deoxygenation;
3)使用凝胶渗透色谱(GPC)监测聚合物分子量,当分子量达到1000-50000Da特定值时停止反应;3) Use gel permeation chromatography (GPC) to monitor the molecular weight of the polymer, and stop the reaction when the molecular weight reaches a specific value of 1000-50000Da;
4)对产物进行提纯,得到分子量在1000-50000Da的线性-非线性嵌段聚合物;4) Purify the product to obtain a linear-nonlinear block polymer with a molecular weight of 1000-50000Da;
5)通过核磁共振氢谱(1HNMR)与凝胶渗透色谱(GPC)确定聚合物的组成、结构、分子量和分子量分布。5) Determine the composition, structure, molecular weight and molecular weight distribution of the polymer by hydrogen nuclear magnetic resonance spectroscopy ( 1 HNMR) and gel permeation chromatography (GPC).
通过上述制备方法制得的线性-非线性嵌段聚合物,由线性聚合物链段和多乙烯基单体聚合的非线性结构构成,其化学结构式如下:The linear-nonlinear block polymer prepared by the above preparation method is composed of a linear polymer segment and a non-linear structure polymerized by polyvinyl monomers, and its chemical structural formula is as follows:
式中,m=5~20,p=5~100,q=5~100;R1结构可以是以下两种:In the formula, m=5~20, p=5~100, q=5~100; R 1 structure can be the following two kinds:
1)*Br;2) 1) *Br; 2)
式中R2结构可以是以下两种:In the formula, the R2 structure can be the following two types:
1) 1)
2) 2)
式中,n=10~200。In the formula, n=10-200.
具体实施例如下:Specific examples are as follows:
实施例1Example 1
基于RAFT聚合机理进行:先将二乙烯基苯(DVB,1.3019g,10mmol)在反应瓶中用50mL的2-丁酮充分溶解,再加入大分子RAFT试剂mPEG-CPADB(Mw=5000Da,250mg,0.05mmol)和引发剂(AIBN,2.73mg,0.0167mmol)搅拌混合。所得反应体系在室温下采用氩气置换除氧的方法除去反应体系中的溶解氧和瓶中空气,置换除氧时间为30min。除氧结束后于80℃进行反应,GPC监测分子量。反应9.5h后停止反应,淬灭自由基。对产物进行沉淀法提纯,并得到分子量为20000Da的线性-非线性嵌段聚合物,其合成示意图参见图3,性能测试结果如下:Based on the mechanism of RAFT polymerization: First, fully dissolve divinylbenzene (DVB, 1.3019g, 10mmol) in a reaction flask with 50mL of 2-butanone, then add the macromolecular RAFT reagent mPEG-CPADB (Mw=5000Da, 250mg, 0.05mmol) and initiator (AIBN, 2.73mg, 0.0167mmol) were stirred and mixed. The obtained reaction system was deoxygenated by argon replacement at room temperature to remove dissolved oxygen and air in the bottle, and the deoxygenation time was 30 minutes. After deoxygenation was completed, the reaction was carried out at 80° C., and the molecular weight was monitored by GPC. After 9.5 hours of reaction, the reaction was stopped to quench free radicals. The product was purified by precipitation method, and a linear-nonlinear block polymer with a molecular weight of 20000Da was obtained. The synthesis schematic diagram is shown in Figure 3, and the performance test results are as follows:
参见图1,为本发明制得的大分子RAFT试剂mPEG-CPABD合成前后GPC谱图,从图中可以知,反应后出峰时间明显左移,分子量增大,分子量增量与CPABD分子量相符,证明实现了mPEG与CPABD的偶合。Referring to Fig. 1, it is the GPC spectrogram before and after the synthesis of the macromolecular RAFT reagent mPEG-CPABD that the present invention makes, can know from the figure, after the reaction, the peak time obviously shifts to the left, the molecular weight increases, and the molecular weight increment is consistent with the CPABD molecular weight, It was demonstrated that the coupling of mPEG to CPABD was achieved.
参见图7,为本发明实施例1反应过程中线性-非线性嵌段聚合物分子量变化GPC谱图,从图中可知,随着反应的进行分子量线性增加,聚合物分子量分布未出现明显增大,即未出现分子间交联,反应可以实现对聚合的良好控制。Referring to Fig. 7, it is the GPC spectrogram of the molecular weight change of the linear-nonlinear block polymer in the reaction process of Example 1 of the present invention. It can be seen from the figure that the molecular weight increases linearly with the progress of the reaction, and the molecular weight distribution of the polymer does not increase significantly. , that is, no intermolecular cross-linking occurs, and the reaction can achieve good control over the polymerization.
参见图9,为本发明实施例1线性-非线性嵌段聚合物聚合过程动力学拟合曲线,从图中可知,反应时间与ln([M]0/[M]t)线性相关,其中,[M]0为反应初始单体浓度,[M]t为与反应时间相对应的t时刻的单体浓度,则该反应满足一级动力学模型。Referring to Fig. 9, it is the kinetic fitting curve of the linear-nonlinear block polymer polymerization process in Example 1 of the present invention. It can be seen from the figure that the reaction time is linearly related to ln([M] 0 /[M] t ), where , [M] 0 is the initial monomer concentration of the reaction, and [M] t is the monomer concentration at time t corresponding to the reaction time, then the reaction satisfies the first-order kinetic model.
实施例2Example 2
基于ATRP聚合机理进行:将双酚A聚氧乙烯醚二丙烯酸酯(BEDA,314.28mg,2mmol)、大分子ATRP引发剂mPEG-BrBased on ATRP polymerization mechanism: bisphenol A polyoxyethylene ether diacrylate (BEDA, 314.28mg, 2mmol), macromolecular ATRP initiator mPEG-Br
(Mw=2000Da,40mg,0.02mmol)、配体N,N,N',N”,N”-五甲基二乙烯基三胺(PMDETA,2.7728mg,0.016mmol)和催化剂CuBr2(0.8934mg,0.004mmol)用20mL二甲基亚砜(DMSO)溶解于50mL的烧瓶中,在室温下用氩气鼓泡除氧30min。取5cm铜线缠于磁子上,在浓盐酸中浸泡20min,取出后用丙酮和水反复冲洗并擦净迅速在氮气保护氛围下放入反应烧瓶,再进行短暂除氧,然后在25℃下进行反应并进行GPC监测。反应3h后停止反应,对产物进行沉淀法提纯,得到分子量为15000Da的线性-非线性嵌段聚合物,其合成示意图参见图4,性能测试结果如下:(Mw=2000Da, 40mg, 0.02mmol), ligand N,N,N',N",N"-pentamethyldivinyltriamine (PMDETA, 2.7728mg, 0.016mmol) and catalyst CuBr 2 (0.8934mg , 0.004mmol) was dissolved in 20mL dimethyl sulfoxide (DMSO) in a 50mL flask, and deoxygenated by bubbling argon for 30min at room temperature. Take a 5cm copper wire and wind it on the magnet, soak it in concentrated hydrochloric acid for 20 minutes, take it out, rinse it repeatedly with acetone and water and wipe it clean, quickly put it into the reaction flask under a nitrogen protective atmosphere, and then perform a short deoxygenation, and then put it in the reaction flask at 25°C Reactions were run and monitored by GPC. After 3 hours of reaction, the reaction was stopped, and the product was purified by precipitation to obtain a linear-nonlinear block polymer with a molecular weight of 15,000 Da. The synthesis schematic diagram is shown in Figure 4, and the performance test results are as follows:
参见图2,为本发明制得的大分子ATRP引发剂mPEG-Br合成前后GPC谱图,从图中可知,反应后出峰时间明显左移,分子量增大,分子量增量与2-溴异丁酰溴(BIB)取代部分分子量相符,证明成功实现了mPEG-Br的合成。Referring to Fig. 2, it is the GPC spectrogram before and after the synthesis of the macromolecular ATRP initiator mPEG-Br that the present invention makes, as can be seen from the figure, after the reaction, the peak time obviously shifts to the left, the molecular weight increases, and the molecular weight increment is the same as that of 2-bromoiso Butyryl bromide (BIB) substituted some molecular weights, which proved the successful synthesis of mPEG-Br.
参见图8,为本发明实施例2反应过程中线性-非线性嵌段聚合物分子量变化GPC谱图,从图中可知,随着反应的进行分子量线性增加,聚合物分子量分布未出现明显增大,即未出现分子间交联,反应可以实现对聚合的良好控制。Referring to Fig. 8, it is the GPC spectrogram of the molecular weight change of the linear-nonlinear block polymer in the reaction process of Example 2 of the present invention. It can be seen from the figure that the molecular weight increases linearly with the progress of the reaction, and the molecular weight distribution of the polymer does not increase significantly. , that is, no intermolecular cross-linking occurs, and the reaction can achieve good control over the polymerization.
以上内容仅为说明本发明的技术思想,不能以此限定本发明的保护范围,凡是按照本发明提出的技术思想,在技术方案基础上所做的任何改动,均落入本发明权利要求书的保护范围之内。The above content is only to illustrate the technical ideas of the present invention, and cannot limit the protection scope of the present invention. Any changes made on the basis of the technical solutions according to the technical ideas proposed in the present invention shall fall within the scope of the claims of the present invention. within the scope of protection.
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