CN106008797A - Polyacrylonitrile gradient copolymer and controllable synthesis method thereof - Google Patents
Polyacrylonitrile gradient copolymer and controllable synthesis method thereof Download PDFInfo
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- 229920000028 Gradient copolymer Polymers 0.000 title claims abstract description 32
- 229920002239 polyacrylonitrile Polymers 0.000 title claims abstract description 32
- 238000001308 synthesis method Methods 0.000 title abstract description 6
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000009826 distribution Methods 0.000 claims abstract description 13
- 239000000178 monomer Substances 0.000 claims abstract description 11
- 239000002904 solvent Substances 0.000 claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 10
- 239000003999 initiator Substances 0.000 claims abstract description 10
- 239000002184 metal Substances 0.000 claims abstract description 10
- 229910052751 metal Inorganic materials 0.000 claims abstract description 10
- -1 comonomer Substances 0.000 claims abstract description 6
- 238000010189 synthetic method Methods 0.000 claims description 10
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical group COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 8
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-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 5
- ROFVEXUMMXZLPA-UHFFFAOYSA-N Bipyridyl Chemical group N1=CC=CC=C1C1=CC=CC=N1 ROFVEXUMMXZLPA-UHFFFAOYSA-N 0.000 claims description 4
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 239000010949 copper Substances 0.000 claims description 4
- CRRUGYDDEMGVDY-UHFFFAOYSA-N 1-bromoethylbenzene Chemical compound CC(Br)C1=CC=CC=C1 CRRUGYDDEMGVDY-UHFFFAOYSA-N 0.000 claims description 3
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 claims description 3
- AGEZXYOZHKGVCM-UHFFFAOYSA-N benzyl bromide Chemical compound BrCC1=CC=CC=C1 AGEZXYOZHKGVCM-UHFFFAOYSA-N 0.000 claims description 3
- RENMDAKOXSCIGH-UHFFFAOYSA-N Chloroacetonitrile Chemical compound ClCC#N RENMDAKOXSCIGH-UHFFFAOYSA-N 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 2
- CVRXLMUYFMERMJ-UHFFFAOYSA-N N,N,N',N'-tetrakis(2-pyridylmethyl)ethylenediamine Chemical compound C=1C=CC=NC=1CN(CC=1N=CC=CC=1)CCN(CC=1N=CC=CC=1)CC1=CC=CC=N1 CVRXLMUYFMERMJ-UHFFFAOYSA-N 0.000 claims description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 2
- KCXMKQUNVWSEMD-UHFFFAOYSA-N benzyl chloride Chemical compound ClCC1=CC=CC=C1 KCXMKQUNVWSEMD-UHFFFAOYSA-N 0.000 claims description 2
- 229940073608 benzyl chloride Drugs 0.000 claims description 2
- JEAVBVKAYUCPAQ-UHFFFAOYSA-N ethyl 2-chloropropanoate Chemical compound CCOC(=O)C(C)Cl JEAVBVKAYUCPAQ-UHFFFAOYSA-N 0.000 claims description 2
- 241001597008 Nomeidae Species 0.000 claims 2
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 claims 2
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 claims 2
- FKRCODPIKNYEAC-UHFFFAOYSA-N ethyl propionate Chemical compound CCOC(=O)CC FKRCODPIKNYEAC-UHFFFAOYSA-N 0.000 claims 2
- UVBFTLVKTGRXER-UHFFFAOYSA-N 1,3,6,10-tetramethyl-1,3,6,10-tetrazacyclododecane Chemical compound CN1CCN(CCCN(CCN(C1)C)C)C UVBFTLVKTGRXER-UHFFFAOYSA-N 0.000 claims 1
- VILCJCGEZXAXTO-UHFFFAOYSA-N 2,2,2-tetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 claims 1
- WOXFMYVTSLAQMO-UHFFFAOYSA-N 2-Pyridinemethanamine Chemical compound NCC1=CC=CC=N1 WOXFMYVTSLAQMO-UHFFFAOYSA-N 0.000 claims 1
- 125000000022 2-aminoethyl group Chemical group [H]C([*])([H])C([H])([H])N([H])[H] 0.000 claims 1
- MHABMANUFPZXEB-UHFFFAOYSA-N O-demethyl-aloesaponarin I Natural products O=C1C2=CC=CC(O)=C2C(=O)C2=C1C=C(O)C(C(O)=O)=C2C MHABMANUFPZXEB-UHFFFAOYSA-N 0.000 claims 1
- 150000001412 amines Chemical class 0.000 claims 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims 1
- 229910052794 bromium Inorganic materials 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 229940113088 dimethylacetamide Drugs 0.000 claims 1
- WDAXFOBOLVPGLV-UHFFFAOYSA-N ethyl isobutyrate Chemical class CCOC(=O)C(C)C WDAXFOBOLVPGLV-UHFFFAOYSA-N 0.000 claims 1
- 239000003205 fragrance Substances 0.000 claims 1
- 239000003863 metallic catalyst Substances 0.000 claims 1
- 150000003462 sulfoxides Chemical class 0.000 claims 1
- 229960001124 trientine Drugs 0.000 claims 1
- 229920000642 polymer Polymers 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 7
- 239000003446 ligand Substances 0.000 abstract description 6
- 238000003786 synthesis reaction Methods 0.000 abstract description 5
- 230000015572 biosynthetic process Effects 0.000 abstract description 4
- 238000006116 polymerization reaction Methods 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 2
- 230000035484 reaction time Effects 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 description 12
- 238000010526 radical polymerization reaction Methods 0.000 description 7
- 229920001577 copolymer Polymers 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 239000003708 ampul Substances 0.000 description 2
- 238000010560 atom transfer radical polymerization reaction Methods 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 230000036632 reaction speed Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000012712 reversible addition−fragmentation chain-transfer polymerization Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- GTLWADFFABIGAE-UHFFFAOYSA-N 1-chloroethylbenzene Chemical group CC(Cl)C1=CC=CC=C1 GTLWADFFABIGAE-UHFFFAOYSA-N 0.000 description 1
- VGUWFGWZSVLROP-UHFFFAOYSA-N 1-pyridin-2-yl-n,n-bis(pyridin-2-ylmethyl)methanamine Chemical compound C=1C=CC=NC=1CN(CC=1N=CC=CC=1)CC1=CC=CC=N1 VGUWFGWZSVLROP-UHFFFAOYSA-N 0.000 description 1
- JNAYPRPPXRWGQO-UHFFFAOYSA-N 2-chloropropanenitrile Chemical compound CC(Cl)C#N JNAYPRPPXRWGQO-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- DGEZNRSVGBDHLK-UHFFFAOYSA-N [1,10]phenanthroline Chemical compound C1=CN=C2C3=NC=CC=C3C=CC2=C1 DGEZNRSVGBDHLK-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- IOLQWGVDEFWYNP-UHFFFAOYSA-N ethyl 2-bromo-2-methylpropanoate Chemical compound CCOC(=O)C(C)(C)Br IOLQWGVDEFWYNP-UHFFFAOYSA-N 0.000 description 1
- ARFLASKVLJTEJD-UHFFFAOYSA-N ethyl 2-bromopropanoate Chemical compound CCOC(=O)C(C)Br ARFLASKVLJTEJD-UHFFFAOYSA-N 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- DWFKOMDBEKIATP-UHFFFAOYSA-N n'-[2-[2-(dimethylamino)ethyl-methylamino]ethyl]-n,n,n'-trimethylethane-1,2-diamine Chemical compound CN(C)CCN(C)CCN(C)CCN(C)C DWFKOMDBEKIATP-UHFFFAOYSA-N 0.000 description 1
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 1
- UKODFQOELJFMII-UHFFFAOYSA-N pentamethyldiethylenetriamine Chemical compound CN(C)CCN(C)CCN(C)C UKODFQOELJFMII-UHFFFAOYSA-N 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- MBYLVOKEDDQJDY-UHFFFAOYSA-N tris(2-aminoethyl)amine Chemical compound NCCN(CCN)CCN MBYLVOKEDDQJDY-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/42—Nitriles
- C08F220/44—Acrylonitrile
-
- 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
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/50—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides selected from alkaline earth metals, zinc, cadmium, mercury, copper or silver
-
- 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
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/72—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44
- C08F4/80—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from iron group metals or platinum group metals
-
- 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
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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)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Polymerization Catalysts (AREA)
Abstract
Description
技术领域technical field
本发明涉及高分子合成技术领域,尤其涉及一种聚丙烯腈梯度共聚物的可控合成方法。The invention relates to the technical field of polymer synthesis, in particular to a controllable synthesis method of a polyacrylonitrile gradient copolymer.
背景技术Background technique
由于“活性”/可控自由基能够对聚合物的结构、分子量、分子量分布进行设计,因而被科学家广泛关注。目前研究较热的主要包括原子转移自由基聚合、可逆加成-断裂链转移聚合和零价金属催化的可控自由基聚合。相对于前两种聚合方法来说,零价金属尤其是零价铜催化的“活性”可控自由基聚合具有反应速度快、反应条件温和以及经济性好的特点,因而被广泛报道。Because "active"/controllable free radicals can design the structure, molecular weight, and molecular weight distribution of polymers, they have attracted widespread attention from scientists. At present, the hot research mainly includes atom transfer radical polymerization, reversible addition-fragmentation chain transfer polymerization and zero-valent metal catalyzed controllable radical polymerization. Compared with the former two polymerization methods, "living" controllable free radical polymerization catalyzed by zero-valent metals, especially zero-valent copper, has the characteristics of fast reaction speed, mild reaction conditions and good economy, so it has been widely reported.
其次,共聚物中重复单元的序列分布对聚合物的性质有很大的影响,因而科学家们不断通过对单元序列分布的控制来提升聚合物的性能。而由于梯度聚合物的组成随着共聚物的链增长会不断的发生变化,因而会给聚合物带来许多优异的性能。Secondly, the sequence distribution of repeating units in copolymers has a great influence on the properties of polymers, so scientists continue to improve the performance of polymers by controlling the sequence distribution of units. And because the composition of the gradient polymer will change continuously with the chain growth of the copolymer, it will bring many excellent properties to the polymer.
众所周知,丙烯腈在合成纤维、合成橡胶以及合成树脂上得到广泛应用,因而研究聚丙烯腈梯度共聚物的性能显得尤为重要。目前关于合成聚丙烯腈梯度共聚物的报道大多数都是基于氮氧稳定自由基聚合、原子转移自由基聚合以及可逆加成-断裂链转移聚合的方法。而通过零价铜催化的“活性”可控自由基聚合来构建聚丙烯腈梯度共聚物的方法至今还没有报道。As we all know, acrylonitrile is widely used in synthetic fibers, synthetic rubber and synthetic resins, so it is particularly important to study the properties of polyacrylonitrile gradient copolymers. Most of the current reports on the synthesis of polyacrylonitrile gradient copolymers are based on nitrogen-oxygen-stabilized radical polymerization, atom transfer radical polymerization and reversible addition-fragmentation chain transfer polymerization. However, the method of constructing polyacrylonitrile gradient copolymers through zero-valent copper-catalyzed "living" controlled free radical polymerization has not been reported so far.
鉴于上述缺陷,本设计人积极加以研究创新,以期创设一种通过零价铜催化的“活性”/可控自由基聚合来构建聚丙烯腈梯度共聚物的合成方法,使其更具有产业上的利用价值。In view of the above-mentioned defects, the designer actively researches and innovates in order to create a synthetic method for constructing polyacrylonitrile gradient copolymers through zero-valent copper-catalyzed "active"/controllable free radical polymerization, making it more industrially useful. use value.
发明内容Contents of the invention
为解决上述技术问题,本发明的目的是提供一种聚丙烯腈梯度共聚物及其可控合成方法,该方法工艺简单、适用单体范围广、合成效率高。In order to solve the above technical problems, the object of the present invention is to provide a polyacrylonitrile gradient copolymer and a controllable synthesis method thereof, which has simple process, wide range of applicable monomers and high synthesis efficiency.
本发明的聚丙烯腈梯度共聚物的可控合成方法,包括以下步骤:将单体丙烯腈、共聚单体、引发剂、零价金属催化剂以及零价金属催化剂的配体置于溶剂中,在25-100℃下,所述单体丙烯腈和共聚单体进行聚合反应,并通过调整反应时间控制得到的聚丙烯腈梯度共聚物的分子量。The controllable synthesis method of polyacrylonitrile gradient copolymer of the present invention comprises the following steps: placing monomer acrylonitrile, comonomer, initiator, zero-valent metal catalyst and the ligand of zero-valent metal catalyst in a solvent, At 25-100°C, the acrylonitrile monomer and the comonomer are polymerized, and the molecular weight of the obtained polyacrylonitrile gradient copolymer is controlled by adjusting the reaction time.
进一步的,所述零价金属催化剂为零价铜或零价铁催化剂。Further, the zero-valent metal catalyst is zero-valent copper or zero-valent iron catalyst.
进一步的,所述单体丙烯腈、共聚单体、配体、引发剂和零价金属催化剂的摩尔比为100-300:100:1-3:1-3:1-3。Further, the molar ratio of the monomer acrylonitrile, comonomer, ligand, initiator and zero-valent metal catalyst is 100-300:100:1-3:1-3:1-3.
进一步的,所述共聚单体与溶剂体积比为100:50-200。Further, the volume ratio of the comonomer to the solvent is 100:50-200.
进一步的,所述共聚单体为甲基丙烯酸甲酯及其衍生物、丙烯酸甲酯及其衍生物和苯乙烯及其衍生物中的一种或几种,如图1所示。Further, the comonomer is one or more of methyl methacrylate and its derivatives, methyl acrylate and its derivatives, and styrene and its derivatives, as shown in FIG. 1 .
进一步的,所述引发剂为α-氯代苯乙烷、α-溴代苯乙烷、苄基氯、苄基溴、α-氯丙酸乙酯、α-溴丙酸乙酯、α-溴代异丁酸乙酯、α-氯乙腈、α-氯丙腈和1-苯基乙基溴中的一种或几种。Further, the initiator is α-chlorophenylethane, α-bromophenylethane, benzyl chloride, benzyl bromide, α-ethyl chloropropionate, α-ethyl bromopropionate, α- One or more of ethyl bromoisobutyrate, α-chloroacetonitrile, α-chloropropionitrile and 1-phenylethyl bromide.
进一步的,所述配体为五甲基二乙烯三胺、六甲基三亚乙基四胺、二乙烯三胺、N,N,N',N'-四(2-吡啶甲基)乙二胺、三(2-吡啶基甲基)胺、三(2-氨基乙基)胺、1,10-菲罗啉、1,4,8,11-四甲基-1,4,8,11-四氮杂环四癸烷和2,2'-联吡啶中的一种或几种。Further, the ligands are pentamethyldiethylenetriamine, hexamethyltriethylenetetramine, diethylenetriamine, N,N,N',N'-tetrakis(2-pyridylmethyl)ethylenediamine Amine, tris(2-pyridylmethyl)amine, tris(2-aminoethyl)amine, 1,10-phenanthroline, 1,4,8,11-tetramethyl-1,4,8,11 - one or more of tetraazacyclotetradecane and 2,2'-bipyridine.
进一步的,所述溶剂为二甲亚砜、N,N-二甲基甲酰胺和N,N-二甲基乙酰胺中的一种或几种。Further, the solvent is one or more of dimethylsulfoxide, N,N-dimethylformamide and N,N-dimethylacetamide.
本发明的聚丙烯腈梯度共聚物,所述聚丙烯腈梯度共聚物的分子量分布系数为Mw/Mn=1.10-1.60In the polyacrylonitrile gradient copolymer of the present invention, the molecular weight distribution coefficient of the polyacrylonitrile gradient copolymer is M w /M n = 1.10-1.60
借由上述方案,本发明具有以下优点:By means of the above scheme, the present invention has the following advantages:
本发明提供了一种聚丙烯腈梯度共聚物的可控合成方法,成功通过零价铜催化的“活性”/可控自由基聚合合成了聚丙烯腈梯度共聚物,相对于现有技术具有反应条件温和、适用共聚单体范围广、反应速率快、产量高等优点,适用于工业化生产;合成得到的聚丙烯腈梯度共聚物的Mw/Mn比值小,表明分子量分布窄,纯度高,所得聚合物的实际分子量和理论分子量相符。The present invention provides a controllable synthesis method of polyacrylonitrile gradient copolymer, which successfully synthesizes polyacrylonitrile gradient copolymer through "active"/controllable free radical polymerization catalyzed by zero-valent copper. Mild conditions, wide range of applicable comonomers, fast reaction rate, high yield, etc., are suitable for industrial production; the Mw / Mn ratio of the synthesized polyacrylonitrile gradient copolymer is small, indicating that the molecular weight distribution is narrow and the purity is high. The actual molecular weight of the polymer is consistent with the theoretical molecular weight.
上述说明仅是本发明技术方案的概述,为了能够更清楚了解本发明的技术手段,并可依照说明书的内容予以实施,以下以本发明的较佳实施例并配合附图详细说明如后。The above description is only an overview of the technical solutions of the present invention. In order to understand the technical means of the present invention more clearly and implement them according to the contents of the description, the preferred embodiments of the present invention and accompanying drawings are described in detail below.
附图说明Description of drawings
图1是本发明中共聚单体的分子结构图;Fig. 1 is the molecular structure diagram of comonomer in the present invention;
图2是本发明中实施例1的聚合物的核磁氢谱图;Fig. 2 is the nuclear magnetic hydrogen spectrogram of the polymer of embodiment 1 in the present invention;
图3是本发明中实施例1与实施例2共聚时单体转化率与分子量以及分子量分布之间的关系图;Fig. 3 is the relationship figure between monomer conversion rate and molecular weight and molecular weight distribution when embodiment 1 and embodiment 2 are copolymerized among the present invention;
图4是本发明中实施例1得到的不同聚丙烯腈梯度共聚物的SEC流出曲线图;Fig. 4 is the SEC outflow curve figure of the different polyacrylonitrile gradient copolymers that embodiment 1 obtains in the present invention;
图5是本发明中实施例2得到的不同聚丙烯腈梯度共聚物的SEC流出曲线图;Fig. 5 is the SEC outflow curve figure of the different polyacrylonitrile gradient copolymers that embodiment 2 obtains in the present invention;
图6是本发明中实施例1所得到的共聚物的组成与转化率的关系图;Fig. 6 is the relation diagram of the composition and the transformation rate of the copolymer obtained in embodiment 1 in the present invention;
图7是得到聚丙烯腈梯度共聚物的结构示意图。Fig. 7 is a schematic diagram of the obtained polyacrylonitrile gradient copolymer.
具体实施方式detailed description
下面结合附图和实施例,对本发明的具体实施方式作进一步详细描述。以下实施例用于说明本发明,但不用来限制本发明的范围。The specific implementation manners of the present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. The following examples are used to illustrate the present invention, but are not intended to limit the scope of the present invention.
实施例1Example 1
依次将丙烯腈0.75mL(11.2mmol)、共聚单体1甲基丙烯酸甲酯0.6mL(5.6mmol)、催化剂铜粉7.2mg(0.112mmol)、引发剂2-溴丙酸乙酯20.2mg(0.112mmol)、配体2,2-联吡啶17.5mg(0.112mmol)和溶剂二甲亚砜1mL加入到反应容器中,加入搅拌子,经过3次标准的冷冻-抽气-解冻充气循环后,在保护气体下封管。将封管后的安瓿瓶置于搅拌器中,在25℃下反应一定时间后,取出封管,打开封管,用少量溶剂溶解后倒入大量沉淀剂中,过夜放置后抽滤、烘干即可得到聚丙烯腈梯度共聚物,其结构示意图如图7所示。Acrylonitrile 0.75mL (11.2mmol), comonomer 1 methyl methacrylate 0.6mL (5.6mmol), catalyst copper powder 7.2mg (0.112mmol), initiator 2-bromopropionate ethyl 20.2mg (0.112 mmol), ligand 2,2-bipyridine 17.5mg (0.112mmol) and solvent dimethyl sulfoxide 1mL were added to the reaction vessel, a stirrer was added, and after 3 standard freeze-pump-thaw inflation cycles, the Protective gas down seal tube. Place the sealed ampoule in a blender, react at 25°C for a certain period of time, take out the sealed tube, open the sealed tube, dissolve it with a small amount of solvent, pour it into a large amount of precipitant, leave it overnight, suction filter, and dry The polyacrylonitrile gradient copolymer can be obtained, and its structural schematic diagram is shown in FIG. 7 .
对聚丙烯腈梯度共聚物作如下测试表征:The polyacrylonitrile gradient copolymer is characterized by the following tests:
如图2所示的核磁氢谱图,从图中可以找到重复单元丙烯腈与甲基丙烯酸甲酯的质子峰,说明两种单体成功接入到聚合物链中;如图3所示,在进行丙烯腈与甲基丙烯酸甲酯共聚时转化率与分子量以及分子量分布之间的关系图,从图中可以看出聚合物的分子量随着转化率的增大而增大,且分子量分布较低;如图4所示的聚丙烯腈梯度共聚物的SEC流出曲线图,从图中发现其流出曲线都呈单峰分布,这些数据都表明聚合过程是“活性”/可控的;图6是所得到的共聚物的组成与转化率的关系图,从图中可以看出随着转化率的增加,共聚物中丙烯腈的单元数不断增多,而甲基丙烯酸甲酯的单元数不断减少,这也说明得到的聚合物为聚丙烯腈梯度共聚物,其结构示意图如图7所示。The proton peaks of the repeating unit acrylonitrile and methyl methacrylate can be found in the NMR spectrum shown in Figure 2, indicating that the two monomers have been successfully inserted into the polymer chain; as shown in Figure 3, The relationship between conversion rate and molecular weight and molecular weight distribution during the copolymerization of acrylonitrile and methyl methacrylate, it can be seen from the figure that the molecular weight of the polymer increases with the increase of conversion rate, and the molecular weight distribution is relatively Low; the SEC efflux curve figure of polyacrylonitrile gradient copolymer as shown in Figure 4, finds that its efflux curve all presents unimodal distribution from the figure, and these data all show that polymerization process is " active "/ controllable; Fig. 6 is the relationship between the composition and conversion rate of the obtained copolymer. It can be seen from the figure that as the conversion rate increases, the number of acrylonitrile units in the copolymer continues to increase, while the number of units of methyl methacrylate decreases continuously. , which also shows that the obtained polymer is a polyacrylonitrile gradient copolymer, and its structural schematic diagram is shown in FIG. 7 .
实施例2Example 2
依次将丙烯腈0.75mL(11.2mmol)、共聚单体1甲基丙烯酸甲酯0.6mL(5.6mmol)、催化剂铜粉7.2mg(0.112mmol)、引发剂2-溴丙酸乙酯20.2mg(0.112mmol)、配体2,2-联吡啶17.5mg(0.112mmol)和溶剂N,N-二甲基甲酰胺1mL加入到反应容器中,加入搅拌子,经过3次标准的冷冻-抽气-解冻充气循环后,在保护气体下封管。将封管后的安瓿瓶置于搅拌器中,在25℃下反应一定时间后,取出封管,打开封管,用少量溶剂溶解后倒入大量沉淀剂中,过夜放置后抽滤、烘干即可得到聚丙烯腈梯度共聚物。Acrylonitrile 0.75mL (11.2mmol), comonomer 1 methyl methacrylate 0.6mL (5.6mmol), catalyst copper powder 7.2mg (0.112mmol), initiator 2-bromopropionate ethyl 20.2mg (0.112 mmol), ligand 2,2-bipyridine 17.5mg (0.112mmol) and solvent N,N-dimethylformamide 1mL were added to the reaction vessel, a stirrer was added, and after 3 standard freezing-pumping-thawing After the inflation cycle, the tube is sealed under protective gas. Place the sealed ampoule in a blender, react at 25°C for a certain period of time, take out the sealed tube, open the sealed tube, dissolve it with a small amount of solvent, pour it into a large amount of precipitant, leave it overnight, suction filter, and dry The polyacrylonitrile gradient copolymer can be obtained.
对聚丙烯腈梯度共聚物作如下测试表征:The polyacrylonitrile gradient copolymer is characterized by the following tests:
如图3所示,在进行丙烯腈与甲基丙烯酸甲酯共聚时转化率与分子量以及分子量分布之间的关系图,从图中可以看出聚合物的分子量随着转化率的增大而增大,且分子量分布较低;图5为得到聚丙烯腈梯度共聚物的SEC流出曲线图,从图中发现其流出曲线都呈单峰分布,这些数据都表明聚合过程是“活性”/可控的。As shown in Figure 3, the relationship between conversion rate and molecular weight and molecular weight distribution when carrying out acrylonitrile and methyl methacrylate copolymerization, it can be seen from the figure that the molecular weight of the polymer increases with the increase of conversion rate Large, and the molecular weight distribution is low; Figure 5 is the SEC efflux curve of the polyacrylonitrile gradient copolymer, from which it is found that the efflux curves are all unimodal, and these data indicate that the polymerization process is "active"/controllable of.
综上,本发明成功基于零价金属催化的“活性”/可控自由基聚合构建了聚丙烯腈梯度共聚物,且该方法反应速度快,反应条件温和。In summary, the present invention successfully constructs polyacrylonitrile gradient copolymers based on zero-valent metal-catalyzed "active"/controllable free radical polymerization, and the method has a fast reaction speed and mild reaction conditions.
以上所述仅是本发明的优选实施方式,并不用于限制本发明,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明技术原理的前提下,还可以做出若干改进和变型,这些改进和变型也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, and is not intended to limit the present invention. It should be pointed out that for those of ordinary skill in the art, some improvements can be made without departing from the technical principle of the present invention. and modifications, these improvements and modifications should also be considered as the protection scope of the present invention.
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