CN100418992C - Preparation method of a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths - Google Patents
Preparation method of a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths Download PDFInfo
- Publication number
- CN100418992C CN100418992C CNB2006100398300A CN200610039830A CN100418992C CN 100418992 C CN100418992 C CN 100418992C CN B2006100398300 A CNB2006100398300 A CN B2006100398300A CN 200610039830 A CN200610039830 A CN 200610039830A CN 100418992 C CN100418992 C CN 100418992C
- Authority
- CN
- China
- Prior art keywords
- hydrophilic
- hydrophobic
- graft polymer
- chain
- macromolecular chain
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 229920000578 graft copolymer Polymers 0.000 title claims abstract description 51
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 34
- 239000000178 monomer Substances 0.000 claims abstract description 23
- 229920002125 Sokalan® Polymers 0.000 claims abstract description 22
- 239000003999 initiator Substances 0.000 claims abstract description 16
- 229920002845 Poly(methacrylic acid) Polymers 0.000 claims abstract description 15
- 239000004584 polyacrylic acid Substances 0.000 claims abstract description 13
- 239000004793 Polystyrene Substances 0.000 claims abstract description 11
- 125000005843 halogen group Chemical group 0.000 claims abstract description 11
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 10
- 229920000058 polyacrylate Polymers 0.000 claims abstract description 10
- 229920002223 polystyrene Polymers 0.000 claims abstract description 10
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims abstract description 8
- 238000010534 nucleophilic substitution reaction Methods 0.000 claims abstract description 8
- 230000002378 acidificating effect Effects 0.000 claims abstract description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 20
- 238000006243 chemical reaction Methods 0.000 claims description 19
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 13
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 12
- 229920000642 polymer Polymers 0.000 claims description 11
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 10
- 238000006116 polymerization reaction Methods 0.000 claims description 10
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 8
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims description 8
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 8
- 230000035484 reaction time Effects 0.000 claims description 8
- 239000002904 solvent Substances 0.000 claims description 8
- 229910021591 Copper(I) chloride Inorganic materials 0.000 claims description 7
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 claims description 7
- 230000007062 hydrolysis Effects 0.000 claims description 7
- ISXSCDLOGDJUNJ-UHFFFAOYSA-N tert-butyl prop-2-enoate Chemical compound CC(C)(C)OC(=O)C=C ISXSCDLOGDJUNJ-UHFFFAOYSA-N 0.000 claims description 7
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 6
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 6
- 229910021589 Copper(I) bromide Inorganic materials 0.000 claims description 5
- ARFLASKVLJTEJD-UHFFFAOYSA-N ethyl 2-bromopropanoate Chemical compound CCOC(=O)C(C)Br ARFLASKVLJTEJD-UHFFFAOYSA-N 0.000 claims description 5
- ROFVEXUMMXZLPA-UHFFFAOYSA-N Bipyridyl Chemical compound N1=CC=CC=C1C1=CC=CC=N1 ROFVEXUMMXZLPA-UHFFFAOYSA-N 0.000 claims description 4
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims description 4
- -1 aromatic sulfonyl chloride class Chemical class 0.000 claims description 4
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 3
- KWYHDKDOAIKMQN-UHFFFAOYSA-N N,N,N',N'-tetramethylethylenediamine Chemical group CN(C)CCN(C)C KWYHDKDOAIKMQN-UHFFFAOYSA-N 0.000 claims description 3
- 150000001350 alkyl halides Chemical class 0.000 claims description 3
- 230000001939 inductive effect Effects 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 125000004429 atom Chemical group 0.000 claims description 2
- NKNDPYCGAZPOFS-UHFFFAOYSA-M copper(i) bromide Chemical compound Br[Cu] NKNDPYCGAZPOFS-UHFFFAOYSA-M 0.000 claims description 2
- 229940045803 cuprous chloride Drugs 0.000 claims description 2
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- FQFILJKFZCVHNH-UHFFFAOYSA-N tert-butyl n-[3-[(5-bromo-2-chloropyrimidin-4-yl)amino]propyl]carbamate Chemical compound CC(C)(C)OC(=O)NCCCNC1=NC(Cl)=NC=C1Br FQFILJKFZCVHNH-UHFFFAOYSA-N 0.000 claims 4
- 238000009736 wetting Methods 0.000 claims 4
- 239000003795 chemical substances by application Substances 0.000 claims 3
- JHUUPUMBZGWODW-UHFFFAOYSA-N 3,6-dihydro-1,2-dioxine Chemical compound C1OOCC=C1 JHUUPUMBZGWODW-UHFFFAOYSA-N 0.000 claims 2
- 108010009736 Protein Hydrolysates Proteins 0.000 claims 2
- 238000004090 dissolution Methods 0.000 claims 2
- 208000021302 gastroesophageal reflux disease Diseases 0.000 claims 2
- 238000010526 radical polymerization reaction Methods 0.000 claims 2
- 238000000967 suction filtration Methods 0.000 claims 2
- RJUFJBKOKNCXHH-UHFFFAOYSA-N Methyl propionate Chemical group CCC(=O)OC RJUFJBKOKNCXHH-UHFFFAOYSA-N 0.000 claims 1
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims 1
- 230000021615 conjugation Effects 0.000 claims 1
- 238000001816 cooling Methods 0.000 claims 1
- 150000002148 esters Chemical class 0.000 claims 1
- QATBRNFTOCXULG-UHFFFAOYSA-N n'-[2-(methylamino)ethyl]ethane-1,2-diamine Chemical compound CNCCNCCN QATBRNFTOCXULG-UHFFFAOYSA-N 0.000 claims 1
- 230000003252 repetitive effect Effects 0.000 claims 1
- 238000005201 scrubbing Methods 0.000 claims 1
- DCKVNWZUADLDEH-UHFFFAOYSA-N sec-butyl acetate Chemical compound CCC(C)OC(C)=O DCKVNWZUADLDEH-UHFFFAOYSA-N 0.000 claims 1
- 230000007704 transition Effects 0.000 claims 1
- 238000010560 atom transfer radical polymerization reaction Methods 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 11
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 24
- 230000015572 biosynthetic process Effects 0.000 description 10
- 238000003786 synthesis reaction Methods 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 9
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 8
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 239000007795 chemical reaction product Substances 0.000 description 6
- 230000008014 freezing Effects 0.000 description 6
- 238000007710 freezing Methods 0.000 description 6
- 238000010257 thawing Methods 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 239000008139 complexing agent Substances 0.000 description 4
- 230000003301 hydrolyzing effect Effects 0.000 description 4
- 229920002521 macromolecule Polymers 0.000 description 4
- ACEONLNNWKIPTM-UHFFFAOYSA-N methyl 2-bromopropanoate Chemical group COC(=O)C(C)Br ACEONLNNWKIPTM-UHFFFAOYSA-N 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- UKODFQOELJFMII-UHFFFAOYSA-N pentamethyldiethylenetriamine Chemical compound CN(C)CCN(C)CCN(C)C UKODFQOELJFMII-UHFFFAOYSA-N 0.000 description 3
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000004005 microsphere Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 229920000193 polymethacrylate Polymers 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- SJMYWORNLPSJQO-UHFFFAOYSA-N tert-butyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC(C)(C)C SJMYWORNLPSJQO-UHFFFAOYSA-N 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical group [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
- 238000012377 drug delivery Methods 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 229920001600 hydrophobic polymer Polymers 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 239000000075 oxide glass Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920005553 polystyrene-acrylate Polymers 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- YBBRCQOCSYXUOC-UHFFFAOYSA-N sulfuryl dichloride Chemical compound ClS(Cl)(=O)=O YBBRCQOCSYXUOC-UHFFFAOYSA-N 0.000 description 1
- UOHMMEJUHBCKEE-UHFFFAOYSA-N tetramethylbenzene Natural products CC1=CC=C(C)C(C)=C1C UOHMMEJUHBCKEE-UHFFFAOYSA-N 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Graft Or Block Polymers (AREA)
Abstract
一种主、侧链长度均可控的亲水-疏水性接枝聚合物的制备方法,属于接枝聚合物制备技术领域。本发明为由原子转移自由基聚合法合成了相对分子质量分布≤1.2的聚苯乙烯(PSt)与聚丙烯酸酯类疏水性大分子链;通过在酸性条件下的水解反应,得到了相对分子质量可控且分布窄的聚甲基丙烯酸或聚丙烯酸亲水性大分子链;在溶液中利用疏水性大分子链末端的卤原子与亲水性大分子链侧基上的羧基进行亲核取代反应,将疏水链“组装”到亲水链上形成亲水-疏水性接枝聚合物;通过调节引发剂与单体的配比可对大分子链的长度进行控制。选用具有不同长度的亲水性链作主链、不同长度的疏水性链进行“组装”,即可制备主、侧链长度可控的亲水-疏水性接枝聚合物。The invention discloses a method for preparing a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths, belonging to the technical field of graft polymer preparation. The present invention synthesizes polystyrene (PSt) and polyacrylate hydrophobic macromolecular chains with relative molecular mass distribution ≤ 1.2 by atom transfer radical polymerization; obtains relative molecular mass through hydrolysis reaction under acidic conditions Controllable and narrowly distributed polymethacrylic acid or polyacrylic acid hydrophilic macromolecular chain; use the halogen atom at the end of the hydrophobic macromolecular chain to carry out nucleophilic substitution reaction with the carboxyl group on the side group of the hydrophilic macromolecular chain in solution , The hydrophobic chain is "assembled" on the hydrophilic chain to form a hydrophilic-hydrophobic graft polymer; the length of the macromolecular chain can be controlled by adjusting the ratio of the initiator to the monomer. Hydrophilic-hydrophobic graft polymers with controllable main and side chain lengths can be prepared by selecting hydrophilic chains with different lengths as the main chain and hydrophobic chains with different lengths for "assembly".
Description
技术领域 technical field
一种主、侧链长度均可控的亲水-疏水性接枝聚合物的制备方法,属于接枝聚合物制备技术领域。通过原子转移自由基聚合方法合成分子链长度可控、末端含有卤素原子的疏水性大分子链,通过在酸性条件下水解聚甲基丙烯酸叔丁酯(或聚丙烯酸叔丁酯)制备聚甲基丙烯酸(或聚丙烯酸),改变原子转移自由基聚合中单体与引发剂的配比来控制疏水性大分子链的长度,选择不同长度的上述疏水性大分子链水解可得到具有不同长度的聚甲基丙烯酸(或聚丙烯酸)亲水性大分子链;通过疏水性大分子链末端的卤原子与亲水性大分子链侧基的羧基之间的亲核取代反应成功“组装”了接枝聚合物。这种亲水-疏水性聚合物可进一步在选择性溶剂中进行自组装形成结构规则的核壳结构微球,改变疏水链与亲水链的比例以及长度,可达到改变微球尺寸及表面羧基含量的目的。The invention discloses a method for preparing a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths, belonging to the technical field of graft polymer preparation. Hydrophobic macromolecular chains with controllable molecular chain length and halogen atoms at the end were synthesized by atom transfer radical polymerization, and polymethacrylate was prepared by hydrolyzing poly-tert-butyl methacrylate (or poly-tert-butyl acrylate) under acidic conditions. Acrylic acid (or polyacrylic acid), change the ratio of monomer and initiator in the atom transfer radical polymerization to control the length of the hydrophobic macromolecular chain, select the hydrolysis of the above-mentioned hydrophobic macromolecular chain of different lengths to obtain polymers with different lengths Methacrylic acid (or polyacrylic acid) hydrophilic macromolecular chain; the grafting was successfully "assembled" through the nucleophilic substitution reaction between the halogen atom at the end of the hydrophobic macromolecular chain and the carboxyl group of the side group of the hydrophilic macromolecular chain polymer. This hydrophilic-hydrophobic polymer can be further self-assembled in a selective solvent to form a regular core-shell structure microsphere, changing the ratio and length of the hydrophobic chain to the hydrophilic chain, and changing the size of the microsphere and the carboxyl group on the surface. content purpose.
背景技术 Background technique
接枝聚合物在特定溶剂中能够进行自组装形成稳定的颗粒,在药物输送与释放、功能化材料方面具有广阔的应用前景。接枝聚合物可由多种方法制备得到,但通过单纯的聚合反应有时难以得到规整的聚合体,通过高分子链与分子之间的相互作用在高分子链中引入所需的小分子或大分子结构的方法,逐渐得到研究和应用。原子转移自由基聚合(ATRP)是近几年兴起的一种聚合方法,通过ATRP方法能够得到相对分子质量可控、相对分子质量分布很窄的聚合物,是制备含有特定基团聚合物的理想选择,如得到末端含有一个卤原子(氯或溴原子)的分子链。本发明即是利用疏水性大分子链末端的卤原子与水解得到的聚甲基丙烯酸(或聚丙烯酸)的侧基羧基进行亲核取代,实现将疏水性大分子链“组装”到亲水性主链上的目的,制备出以亲水性聚甲基丙烯酸或聚丙烯酸为主干,疏水性大分子链为侧枝的亲水-疏水性接枝聚合物。Grafted polymers can self-assemble in specific solvents to form stable particles, and have broad application prospects in drug delivery and release, and functionalized materials. Grafted polymers can be prepared by a variety of methods, but sometimes it is difficult to obtain a regular polymer through a simple polymerization reaction, and the required small molecules or macromolecules are introduced into the polymer chain through the interaction between the polymer chain and the molecule. The method of structure has gradually been researched and applied. Atom Transfer Radical Polymerization (ATRP) is a polymerization method that has emerged in recent years. Through the ATRP method, polymers with controllable molecular weight and narrow molecular weight distribution can be obtained. It is an ideal method for preparing polymers containing specific groups. Selection, such as obtaining a molecular chain with a halogen atom (chlorine or bromine atom) at the end. The present invention uses the halogen atom at the end of the hydrophobic macromolecular chain to carry out nucleophilic substitution with the side group carboxyl group of polymethacrylic acid (or polyacrylic acid) obtained by hydrolysis, so as to realize the "assembly" of the hydrophobic macromolecular chain into the hydrophilic The purpose on the main chain is to prepare a hydrophilic-hydrophobic graft polymer with hydrophilic polymethacrylic acid or polyacrylic acid as the backbone and hydrophobic macromolecular chains as side branches.
发明内容 Contents of the invention
本发明的目的是提供一种主、侧链长度均可控的亲水-疏水性接枝聚合物的制备方法,通过原子转移自由基聚合方法,分别合成分子量可控的疏水性大分子链;由于甲基丙烯酸叔丁酯或丙烯酸叔丁酯的侧基叔丁基易水解转变为羧基,通过在酸性条件下水解聚甲基丙烯酸叔丁酯或丙烯酸叔丁酯得到长度可控的亲水性大分子链聚甲基丙烯酸或聚丙烯酸,继续进行亲核取代反应制备得到主链、侧链长度可控的亲水-疏水性接枝聚合物。The purpose of the present invention is to provide a method for preparing a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths, and synthesize hydrophobic macromolecular chains with controllable molecular weights respectively by atom transfer radical polymerization; Since the pendant tert-butyl group of tert-butyl methacrylate or tert-butyl acrylate is easily hydrolyzed into a carboxyl group, the length-controllable hydrophilicity can be obtained by hydrolyzing poly-tert-butyl methacrylate or tert-butyl acrylate under acidic conditions The macromolecular chain polymethacrylic acid or polyacrylic acid is continuously subjected to nucleophilic substitution reaction to prepare a hydrophilic-hydrophobic graft polymer with controllable main chain and side chain length.
本发明的技术方案:Technical scheme of the present invention:
由原子转移自由基聚合法合成聚苯乙烯PSt或聚丙烯酸酯类(聚甲基丙烯酸甲酯PMMA、聚甲基丙烯酸叔丁酯PtBMA、聚丙烯酸叔丁酯PtBA、聚甲基丙烯酸正丁酯PnBMA、聚丙烯酸正丁酯PnBA等)疏水性大分子链;通过使PtBMA或PtBA在酸性条件下水解,得到聚甲基丙烯酸PMAA或聚丙烯酸PAA亲水性大分子链;在溶液中利用疏水性大分子链末端的卤原子与亲水性大分子链侧基上的羧基进行亲核取代反应,形成亲水-疏水性接枝聚合物,其通式为:Synthesis of polystyrene PSt or polyacrylates (polymethyl methacrylate PMMA, poly tert-butyl methacrylate PtBMA, poly tert-butyl acrylate PtBA, poly-n-butyl methacrylate PnBMA) by atom transfer radical polymerization , poly(n-butyl acrylate, PnBA, etc.) hydrophobic macromolecular chain; by hydrolyzing PtBMA or PtBA under acidic conditions, polymethacrylic acid PMAA or polyacrylic acid PAA hydrophilic macromolecular chain; The halogen atom at the end of the molecular chain undergoes a nucleophilic substitution reaction with the carboxyl group on the side group of the hydrophilic macromolecular chain to form a hydrophilic-hydrophobic graft polymer. The general formula is:
式中,20≤n≤200,20≤m≤200,p表示取代程度,p的范围为5%-20%。R为H,CH3,R1为COOCH3,COOC(CH3)3,COO(CH2)3CH3。R2为H,CH3。In the formula, 20≤n≤200, 20≤m≤200, p represents the degree of substitution, and the range of p is 5%-20%. R is H, CH 3 , R 1 is COOCH 3 , COOC(CH 3 ) 3 , COO(CH 2 ) 3 CH 3 . R2 is H, CH3 .
疏水性大分子链的制备,其反应式如下:The preparation of hydrophobic macromolecular chain, its reaction formula is as follows:
式中X为Cl或Br。In the formula, X is Cl or Br.
原子转移自由基聚合方法是利用含卤化合物(从理论上讲,α位上含有诱导共轭基团的卤代烷或芳香磺酰氯类物质都可作ATRP引发剂),在过渡金属与配位化合物形成的配位体系中,实现休眠种与活性种的快速平衡,从而使单体聚合,它能在较温和的条件下完成反应,而且聚合反应稳定,能得到相对分子质量分布很窄的聚合物。ATRP反应中聚合物的相对分子质量直接取决于单体与引发剂的摩尔比。The atom transfer radical polymerization method is to use a halogen-containing compound (in theory, an alkyl halide or an aromatic sulfonyl chloride containing an inductive conjugated group at the α position can be used as an ATRP initiator), and the transition metal and the coordination compound are formed In the coordination system, the rapid balance of dormant species and active species can be achieved, so that the monomer can be polymerized. It can complete the reaction under milder conditions, and the polymerization reaction is stable, and a polymer with a relatively narrow molecular mass distribution can be obtained. The relative molecular mass of the polymer in the ATRP reaction depends directly on the molar ratio of monomer to initiator.
疏水性大分子链的制备方法,是以疏水性单体为聚合单体,选择有特定结构的引发剂,在配位剂和催化剂存在下进行原子转移自由基聚合反应而制得疏水性大分子链,改变单体与引发剂的摩尔比控制大分子链的相对分子质量。The preparation method of the hydrophobic macromolecular chain is to use the hydrophobic monomer as the polymerization monomer, select the initiator with a specific structure, and carry out the atom transfer radical polymerization reaction in the presence of the complexing agent and the catalyst to prepare the hydrophobic macromolecules Chain, changing the molar ratio of monomer and initiator to control the relative molecular mass of the macromolecular chain.
具体制备工艺为:以疏水性单体为聚合单体,选择α位上含有诱导共轭基团的卤代烷或芳香磺酰氯类物质作引发剂,在配位剂和催化剂存在下进行原子转移自由基聚合反应而制得末端含有卤原子的聚苯乙烯或聚丙烯酸酯类疏水性大分子链,聚合单体∶配位剂∶催化剂∶引发剂的摩尔配比定为n∶1∶2∶1,改变单体与引发剂的摩尔比20≤n≤200达到控制大分子链的相对分子质量,反应温度控制在80~130℃,反应时间控制为6~12小时,配位剂为四甲基乙二胺、五甲基二亚乙基三胺或联二吡啶,催化剂为氯化亚铜、溴化亚铜或氯化亚铁,所述引发剂为α-溴代丙酸甲酯或α-溴代丙酸乙酯。The specific preparation process is: use hydrophobic monomers as polymerization monomers, select haloalkanes or aromatic sulfonyl chlorides containing inductive conjugated groups at the α position as initiators, and carry out atom transfer free radicals in the presence of complexing agents and catalysts Polymerization reaction to obtain polystyrene or polyacrylate hydrophobic macromolecular chains containing halogen atoms at the end, the molar ratio of polymerized monomer: complexing agent: catalyst: initiator is determined as n: 1: 2: 1, Change the molar ratio of the monomer to the initiator to 20≤n≤200 to control the relative molecular mass of the macromolecular chain, control the reaction temperature at 80-130°C, control the reaction time at 6-12 hours, and the complexing agent is tetramethylbenzene Diamine, pentamethyldiethylenetriamine or bipyridine, the catalyst is cuprous chloride, cuprous bromide or ferrous chloride, and the initiator is methyl α-bromopropionate or α- Ethyl bromopropionate.
亲水性大分子链PMAA的制备方法:是以PtBMA为原料进行水解,选择1,4-二氧六环为溶剂溶解PtBMA,加入一定量浓盐酸进行回流。水解反应温度控制在75~95℃,反应时间控制为12~40小时,反应结束,滴加环己烷或正己烷使之沉淀、抽滤,得到水解产物,浓盐酸与1,4-二氧六环的体积比为1∶10~1∶20。The preparation method of the hydrophilic macromolecular chain PMAA includes: hydrolyzing PtBMA as a raw material, selecting 1,4-dioxane as a solvent to dissolve the PtBMA, and adding a certain amount of concentrated hydrochloric acid for reflux. The temperature of the hydrolysis reaction is controlled at 75-95°C, and the reaction time is controlled at 12-40 hours. After the reaction is completed, cyclohexane or n-hexane is added dropwise to precipitate and filtered with suction to obtain the hydrolyzate, concentrated hydrochloric acid and 1,4-dioxine The volume ratio of the hexacyclic rings is 1:10-1:20.
亲水性大分子链PAA的制备方法:是以PtBA为原料进行水解,选择二甲亚砜为溶剂溶解PtBA,加入一定量浓盐酸进行回流。水解反应温度控制在85~95℃,反应时间控制为20~40小时,反应结束,滴加石油醚或正己烷使之沉淀、抽滤,得到水解产物,浓盐酸与二甲亚砜的体积比为1∶10~1∶20。The preparation method of the hydrophilic macromolecular chain PAA is as follows: PtBA is used as a raw material for hydrolysis, dimethyl sulfoxide is selected as a solvent to dissolve the PtBA, and a certain amount of concentrated hydrochloric acid is added for reflux. The hydrolysis reaction temperature is controlled at 85-95°C, and the reaction time is controlled at 20-40 hours. After the reaction is completed, petroleum ether or n-hexane is added dropwise to precipitate and filter with suction to obtain the hydrolyzate. The volume ratio of concentrated hydrochloric acid to dimethyl sulfoxide 1:10 to 1:20.
亲水-疏水性接枝聚合物的合成:在反应容器中依次加入PMAA或PAA,一定量的疏水性大分子链,以N,N-二甲基甲酰胺为溶剂,搅拌充分,加入疏水性大分子链摩尔数的1-5倍量的三乙胺,反应温度控制为30~50℃,反应时间控制为6~20小时,反应结束后自然冷却,静置,收集下层油状物,再用一定量的氯仿或四氢呋喃反复洗涤,除去未反应的高分子,得到亲水-疏水性接枝聚合物。其反应式如下:Synthesis of hydrophilic-hydrophobic graft polymer: Add PMAA or PAA, a certain amount of hydrophobic macromolecular chains to the reaction vessel in sequence, use N,N-dimethylformamide as solvent, stir well, add hydrophobic Triethylamine in an amount of 1-5 times the number of moles of the macromolecular chain, the reaction temperature is controlled at 30-50°C, and the reaction time is controlled at 6-20 hours. After the reaction is completed, it is cooled naturally, left to stand, and the oily substance in the lower layer is collected, and then used A certain amount of chloroform or tetrahydrofuran is repeatedly washed to remove unreacted macromolecules to obtain a hydrophilic-hydrophobic graft polymer. Its reaction formula is as follows:
其中R为H,R1为R2=CH3时,所述亲水-疏水性接枝聚合物为聚甲基丙烯酸-g-聚苯乙烯接枝聚合物。where R is H and R1 is When R 2 =CH 3 , the hydrophilic-hydrophobic graft polymer is polymethacrylic acid-g-polystyrene graft polymer.
其中R为H,R1为COOC(CH3)3,R2=CH3时,所述亲水-疏水性接枝聚合物为聚甲基丙烯酸-g-聚丙烯酸叔丁酯接枝聚合物。Where R is H, R 1 is COOC(CH 3 ) 3 , and R 2 =CH 3 , the hydrophilic-hydrophobic graft polymer is polymethacrylic acid-g-polyacrylate tert-butyl ester graft polymer .
其中R为CH3,R1为COOC(CH3)3,R2=CH3时,所述亲水-疏水性接枝聚合物为聚甲基丙烯酸-g-聚甲基丙烯酸叔丁酯接枝聚合物。Where R is CH 3 , R 1 is COOC(CH 3 ) 3 , and R 2 =CH 3 , the hydrophilic-hydrophobic graft polymer is polymethacrylic acid-g-polymethacrylate tert-butyl ester branch polymer.
其中R为CH3,R1为COOCH3,R2=CH3时,所述亲水-疏水性接枝聚合物为聚甲基丙烯酸-g-聚甲基丙烯酸甲酯接枝聚合物。Where R is CH 3 , R 1 is COOCH 3 , and R 2 =CH 3 , the hydrophilic-hydrophobic graft polymer is polymethacrylic acid-g-polymethylmethacrylate graft polymer.
其中R为CH3,R1为COO(CH2)3CH3,R2=CH3时,所述亲水-疏水性接枝聚合物为聚甲基丙烯酸-g-聚甲基丙烯酸正丁酯接枝聚合物。Where R is CH 3 , R 1 is COO(CH 2 ) 3 CH 3 , and R 2 =CH 3 , the hydrophilic-hydrophobic graft polymer is polymethacrylic acid-g-polymethacrylic acid n-butyl Ester graft polymers.
其中R为H,R1为R2=H时,所述亲水-疏水性接枝聚合物为聚丙烯酸-g-聚苯乙烯接枝聚合物。where R is H and R1 is When R 2 =H, the hydrophilic-hydrophobic graft polymer is polyacrylic acid-g-polystyrene graft polymer.
其中R为H,R1为COOC(CH3)3,R2=H时,所述亲水-疏水性接枝聚合物为聚丙烯酸-g-聚丙烯酸叔丁酯接枝聚合物。Wherein R is H, R 1 is COOC(CH 3 ) 3 , and R 2 =H, the hydrophilic-hydrophobic graft polymer is polyacrylic acid-g-polyacrylate tert-butyl ester graft polymer.
其中R为CH3,R1为COOC(CH3)3,R2=H时,所述亲水-疏水性接枝聚合物为聚丙烯酸-g-聚甲基丙烯酸叔丁酯接枝聚合物。Wherein R is CH 3 , R 1 is COOC(CH 3 ) 3 , and R 2 =H, the hydrophilic-hydrophobic graft polymer is polyacrylic acid-g-poly tert-butyl methacrylate graft polymer .
其中R为CH3,R1为COOCH3,R2=H时,所述亲水-疏水性接枝聚合物为聚丙烯酸-g-聚甲基丙烯酸甲酯接枝聚合物。Where R is CH 3 , R 1 is COOCH 3 , and R 2 =H, the hydrophilic-hydrophobic graft polymer is polyacrylic acid-g-polymethyl methacrylate graft polymer.
其中R为CH3,R1为COO(CH2)3CH3,R2=H时,所述亲水-疏水性接枝聚合物为聚丙烯酸-g-聚甲基丙烯酸正丁酯接枝聚合物。Where R is CH 3 , R 1 is COO(CH 2 ) 3 CH 3 , and R 2 =H, the hydrophilic-hydrophobic graft polymer is polyacrylic acid-g-poly-n-butyl methacrylate grafted polymer.
上述亲核取代反应中,选用具有不同长度的PMAA或PAA做主链、不同长度的疏水性链做侧链,可得到主链、侧链长度不同的亲水-疏水性接枝聚合物。In the above-mentioned nucleophilic substitution reaction, select PMAA or PAA with different lengths as the main chain and hydrophobic chains with different lengths as the side chains to obtain hydrophilic-hydrophobic graft polymers with different lengths of the main chain and side chains.
经表征,各类大分子链分子量可控,相对分子质量分布均匀(Mw/Mn<1.20)。可以通过改变单体与引发剂的摩尔比来可控各类大分子链的相对分子质量。各类亲水-疏水性接枝聚合物结构明确,且接枝程度趋于饱和。After characterization, the molecular weight of various macromolecular chains is controllable, and the relative molecular mass distribution is uniform (M w /M n <1.20). The relative molecular mass of various macromolecular chains can be controlled by changing the molar ratio of monomer and initiator. All kinds of hydrophilic-hydrophobic grafted polymers have clear structures, and the degree of grafting tends to be saturated.
本发明的有益效果:本发明提供了一种制备主链、侧链长度均可控的亲水-疏水性接枝聚合物的方法。由原子转移自由基聚合合成了相对分子质量分布≤1.2的疏水性聚丙烯酸酯类或聚苯乙烯大分子链;通过调节引发剂与单体的配比可对各种高分子链的相对分子质量进行控制,亦即对分子链长度进行控制。进而聚丙烯酸酯类大分子链在酸性条件下水解,制得了相对分子质量分布窄的PMAA或PAA。在溶液中利用疏水性大分子链末端的卤原子与亲水性链侧基上的羧基进行亲核取代反应,将疏水性链“组装”到亲水性链上形成接枝聚合物,可实现枝链数目的初步可控性。Beneficial effects of the present invention: the present invention provides a method for preparing a hydrophilic-hydrophobic graft polymer whose main chain and side chain length can be controlled. Hydrophobic polyacrylate or polystyrene macromolecular chains with a relative molecular mass distribution of ≤1.2 were synthesized by atom transfer radical polymerization; the relative molecular mass of various macromolecular chains can be adjusted by adjusting the ratio of initiator to monomer To control, that is to say, to control the length of the molecular chain. Further, polyacrylate macromolecular chains are hydrolyzed under acidic conditions to produce PMAA or PAA with a narrow relative molecular mass distribution. In the solution, the halogen atom at the end of the hydrophobic macromolecular chain and the carboxyl group on the side group of the hydrophilic chain are used for nucleophilic substitution reaction, and the hydrophobic chain is "assembled" on the hydrophilic chain to form a graft polymer, which can realize Preliminary controllability of branch number.
具体实施方式 Detailed ways
实施例1、疏水性大分子链PtBMA的合成Embodiment 1, the synthesis of hydrophobic macromolecular chain PtBMA
室温下在容器中依次按配比加入五甲基二亚乙基三胺,CuCl,α-溴代丙酸乙酯,单体(根据相对分子质量需要n为50)。搅拌使之充分混合,经过1-5次冷冻、解冻循环,持续通入高纯氮气20-60min后密封。在100℃油浴中反应6小时,取出,自然冷却,以四氢呋喃溶解反应产物,将溶液通过金属氧化物玻璃柱,除去残留的CuCl,滴加进甲醇/水(甲醇/水体积比为1∶1-1∶5)的混合介质中沉淀,过滤,反复操作,真空干燥至恒重,得PtBMA。At room temperature, add pentamethyldiethylenetriamine, CuCl, ethyl α-bromopropionate, and monomers in sequence according to the proportions in the container (according to the relative molecular mass, n is required to be 50). Stir to make it fully mixed, after 1-5 cycles of freezing and thawing, continuously inject high-purity nitrogen for 20-60 minutes and then seal it. React in an oil bath at 100°C for 6 hours, take it out, cool naturally, dissolve the reaction product with tetrahydrofuran, pass the solution through a metal oxide glass column to remove residual CuCl, add dropwise methanol/water (methanol/water volume ratio is 1: 1-1:5) in the mixed medium, filtered, repeated operations, and vacuum-dried to constant weight to obtain PtBMA.
实施例2、疏水性大分子链PSt的合成Embodiment 2, the synthesis of hydrophobic macromolecular chain PSt
室温下在反应容器中依次按配比加入联二吡啶,CuBr,α-溴代丙酸甲酯,单体(根据相对分子质量需要n为200)。搅拌使之充分混合,经过数次冷冻、解冻循环,持续通入高纯氮气45min后密封。在130℃油浴中反应10小时,取出,自然冷却,以环己烷溶解反应产物,将溶液用氧化铝粉末混合洗涤、过滤,除去残留的CuBr,滴加进乙醇介质中沉淀,过滤,反复操作三次,真空干燥至恒重,得PSt。Add bipyridine, CuBr, methyl α-bromopropionate, and monomers sequentially in the reaction vessel according to the ratio at room temperature (n is required to be 200 according to the relative molecular mass). Stir to make it fully mixed, after several cycles of freezing and thawing, continue to pass high-purity nitrogen gas for 45 minutes and then seal it. React in an oil bath at 130°C for 10 hours, take it out, cool naturally, dissolve the reaction product with cyclohexane, mix and wash the solution with alumina powder, filter to remove residual CuBr, drop into ethanol medium to precipitate, filter, repeat The operation was performed three times, and vacuum-dried to constant weight, PSt was obtained.
实施例3、疏水性大分子链PMMA的合成Embodiment 3, the synthesis of hydrophobic macromolecular chain PMMA
室温下在容器中依次按配比加入四甲基乙二胺,FeCl2,α-溴代丙酸甲酯,单体(根据相对分子质量需要n为100)。搅拌使之充分混合,经过数次冷冻、解冻循环,持续通入高纯氮气60min后密封。在80℃油浴中反应8小时,取出,自然冷却,以N,N-二甲基甲酰胺溶解反应产物,将溶液通过氧化铝玻璃柱,除去残留的FeCl2,滴加进乙醇/水(乙醇/水体积比为1∶3-1∶5)的混合介质中沉淀,过滤,反复操作三次,真空干燥至恒重,得PMMA。At room temperature, tetramethylethylenediamine, FeCl 2 , methyl α-bromopropionate, and monomers are sequentially added in proportion to the container (according to the relative molecular mass, n is required to be 100). Stir to make it fully mixed, after several cycles of freezing and thawing, continue to pass high-purity nitrogen gas for 60 minutes and then seal it. React in an oil bath at 80°C for 8 hours, take it out, cool naturally, dissolve the reaction product with N,N-dimethylformamide, pass the solution through an alumina glass column to remove residual FeCl 2 , add dropwise into ethanol/water ( Ethanol/water volume ratio is 1: 3-1: 5) in the mixed medium of precipitation, filter, repeat operation three times, vacuum dry to constant weight, obtain PMMA.
实施例4、疏水性大分子链PtBA的合成Embodiment 4, the synthesis of hydrophobic macromolecular chain PtBA
室温下在烧瓶中依次按配比加入四甲基乙二胺,CuCl,α-溴代丙酸乙酯,单体(根据相对分子质量需要n为20)。搅拌使之充分混合,经过冷冻、解冻循环,持续通入高纯氮气60min后密封。在100℃油浴中反应12小时,结束后自然冷却,以四氢呋喃溶解反应产物,将溶液用氧化铝粉末混合洗涤、过滤,除去残留的CuCl,滴加进甲醇/水(甲醇/水体积比为1∶1-1∶5)的混合介质中沉淀,过滤,反复操作三次,真空干燥至恒重,得PtBA。At room temperature, tetramethylethylenediamine, CuCl, ethyl α-bromopropionate, and monomers are sequentially added in proportion to the flask (according to the relative molecular mass, n is required to be 20). Stir to make it fully mixed, after freezing and thawing cycles, continue to pass high-purity nitrogen gas for 60 minutes and then seal it. React in an oil bath at 100°C for 12 hours, cool naturally after the end, dissolve the reaction product with tetrahydrofuran, mix and wash the solution with alumina powder, filter, remove residual CuCl, add methanol/water dropwise (methanol/water volume ratio is 1:1-1:5) in the mixed medium, filtered, repeated three times, and vacuum-dried to constant weight to obtain PtBA.
实施例5、疏水性大分子链PnBA的合成Embodiment 5, the synthesis of hydrophobic macromolecular chain PnBA
室温下在烧瓶中依次按配比加入五甲基二亚乙基三胺,CuBr,α-溴代丙酸甲酯,单体(根据相对分子质量需要n为75)。搅拌充分,经过冷冻、解冻循环,持续通入高纯氮气60min后密封。在90℃油浴中反应9小时,结束后自然冷却,以二甲亚砜溶解反应产物,将溶液用氧化铝粉末洗涤,除去残留的金属成分,滴加进甲醇/水(甲醇/水体积比为1∶1-1∶5)的混合介质中沉淀,过滤,反复操作三次,真空干燥至恒重,得PnBA。At room temperature, add pentamethyldiethylenetriamine, CuBr, methyl α-bromopropionate, and monomers (n is 75 according to the relative molecular mass) in the flask in sequence. Stir well, go through freezing and thawing cycles, and keep feeding high-purity nitrogen for 60 minutes before sealing. React in an oil bath at 90°C for 9 hours, cool naturally after the end, dissolve the reaction product with dimethyl sulfoxide, wash the solution with alumina powder, remove residual metal components, add methanol/water (methanol/water volume ratio 1:1-1:5) in the mixed medium, filtered, repeated three times, and vacuum-dried to constant weight to obtain PnBA.
实施例6、疏水性大分子链PnBMA的合成Embodiment 6, the synthesis of hydrophobic macromolecular chain PnBMA
室温下在烧瓶中依次按配比加入联二吡啶,CuCl,α-溴代丙酸乙酯,单体(根据相对分子质量需要n为125)。搅拌充分,经过冷冻、解冻循环,持续通入高纯氮气60min后密封。在85℃油浴中反应9小时,结束后自然冷却,以DMSO溶解反应产物,用氧化铝粉末洗涤,除去残留的金属成分,滴加进甲醇/水(甲醇/水体积比为1∶1-1∶5)的混合介质中沉淀,过滤,反复操作三次,真空干燥至恒重,得PnBMA。Add bipyridine, CuCl, ethyl α-bromopropionate, and monomers in the flask in sequence at room temperature (according to the relative molecular mass, n is required to be 125). Stir well, go through freezing and thawing cycles, and keep feeding high-purity nitrogen for 60 minutes before sealing. React in an oil bath at 85°C for 9 hours, cool naturally after the end, dissolve the reaction product with DMSO, wash with alumina powder, remove residual metal components, add methanol/water dropwise (methanol/water volume ratio is 1:1- 1:5) in a mixed medium, filtered, repeated three times, and vacuum-dried to constant weight to obtain PnBMA.
实施例7、亲水性大分子链的合成Embodiment 7, the synthesis of hydrophilic macromolecular chain
在烧瓶中加入PtBMA 1g,用30mL 1,4-二氧六环溶解,再加入1.5-3mL浓盐酸,在75-95℃温度下油浴中回流反应12-40小时,结束后取出样品,滴加环己烷或正己烷使之沉淀、抽滤,真空干燥至恒重,得水解产物。Add 1g of PtBMA to the flask, dissolve it with 30mL of 1,4-dioxane, then add 1.5-3mL of concentrated hydrochloric acid, reflux reaction in an oil bath at 75-95°C for 12-40 hours, take out the sample after the end, drop Add cyclohexane or n-hexane to make it precipitate, filter it with suction, and dry it in vacuum to constant weight to obtain the hydrolyzate.
实施例8、亲水性大分子链的合成Embodiment 8, the synthesis of hydrophilic macromolecular chain
在烧瓶中加入PtBA 1g,用30mL二甲亚砜溶解,再加入1.5-3mL浓盐酸,在85-95℃温度下油浴中回流反应20-40小时,结束后取出样品,滴加石油醚或正己烷使之沉淀、抽滤,真空干燥至恒重,得水解产物。Add 1g of PtBA to the flask, dissolve it with 30mL dimethyl sulfoxide, then add 1.5-3mL concentrated hydrochloric acid, reflux reaction in an oil bath at 85-95°C for 20-40 hours, take out the sample after the end, add petroleum ether or Precipitate with n-hexane, filter with suction, and dry in vacuum until constant weight to obtain the hydrolyzate.
实施例9、亲水-疏水性接枝聚合物的制备Embodiment 9, the preparation of hydrophilic-hydrophobic graft polymer
在容器中依次加入按实施例7或例8水解得到的PMAA或PAA,预定量的疏水性大分子链,DMF 5~20mL,搅拌、溶解,加入三乙胺1~5mL,升温至30~50℃反应6~20小时,冷却、静置,收集下层油状物。再用一定量的氯仿或四氢呋喃反复洗涤,除去未反应的高分子,得到亲水-疏水性接枝聚合物。Add PMAA or PAA obtained by hydrolysis according to Example 7 or Example 8, a predetermined amount of hydrophobic macromolecular chains, DMF 5-20mL, stir and dissolve in the container, add 1-5mL of triethylamine, and heat up to 30-50 ℃ for 6 to 20 hours, cooled, let stand, and collected the lower layer of oil. Repeated washing with a certain amount of chloroform or tetrahydrofuran to remove unreacted macromolecules to obtain a hydrophilic-hydrophobic graft polymer.
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2006100398300A CN100418992C (en) | 2006-04-17 | 2006-04-17 | Preparation method of a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2006100398300A CN100418992C (en) | 2006-04-17 | 2006-04-17 | Preparation method of a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1858079A CN1858079A (en) | 2006-11-08 |
CN100418992C true CN100418992C (en) | 2008-09-17 |
Family
ID=37297039
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2006100398300A Expired - Fee Related CN100418992C (en) | 2006-04-17 | 2006-04-17 | Preparation method of a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN100418992C (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101270202B (en) * | 2007-03-23 | 2010-08-11 | 中国科学院化学研究所 | Polymethyl methacrylate with superhydrophobic surface and preparation method thereof |
CN107903348B (en) * | 2017-11-28 | 2020-06-26 | 常州大学 | A kind of preparation method of polyethylene glycol grafted polymethyl methacrylate amphiphilic graft copolymer |
CN109574743A (en) * | 2018-11-26 | 2019-04-05 | 无锡市天膜新材料有限公司 | A kind of Water Soluble Compound fertilizer anti-caking agent and preparation method thereof |
CN113717322B (en) * | 2021-08-27 | 2022-05-20 | 西安交通大学 | Near molecular weight monodisperse polymer brush and synthesis method thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1709926A (en) * | 2005-06-30 | 2005-12-21 | 江南大学 | Preparation of Poly(tert-Butyl Methacrylate) Macromonomer by Atom Transfer Radical Polymerization |
-
2006
- 2006-04-17 CN CNB2006100398300A patent/CN100418992C/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1709926A (en) * | 2005-06-30 | 2005-12-21 | 江南大学 | Preparation of Poly(tert-Butyl Methacrylate) Macromonomer by Atom Transfer Radical Polymerization |
Non-Patent Citations (2)
Title |
---|
两亲性嵌段共聚物PS-b-PMAA的合成与胶束化行为研究. 华慢,杨伟,薛乔,陈明清,刘晓亚,杨成.化学学报,第63卷第7期. 2005 |
两亲性嵌段共聚物PS-b-PMAA的合成与胶束化行为研究. 华慢,杨伟,薛乔,陈明清,刘晓亚,杨成.化学学报,第63卷第7期. 2005 * |
Also Published As
Publication number | Publication date |
---|---|
CN1858079A (en) | 2006-11-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Matyjaszewski | Advanced materials by atom transfer radical polymerization | |
US7795355B2 (en) | Preparation of functional polymers | |
Arredondo et al. | Synthesis of CO 2-responsive cellulose nanocrystals by surface-initiated Cu (0)-mediated polymerisation | |
CN102702536B (en) | Synthetic method of triblock polymer | |
CN103819584B (en) | A kind of cyclic azobenzene amphiphilic block copolymer and its preparation method | |
CN100579995C (en) | A kind of method of styrene/maleic anhydride copolymerization reaction | |
JP2002540234A (en) | Catalytic method for controlled polymerization of free radically (co) polymerizable monomers and functional polymer systems produced thereby | |
CN100465197C (en) | A kind of preparation method of acrylonitrile homo(co)polymer | |
JPH03195711A (en) | Polymer containing unit derived from maleimide, imprroved in heat resistance | |
CN101691417B (en) | A kind of preparation method of star poly(meth)acrylic acid long-chain ester polymer | |
CN100418992C (en) | Preparation method of a hydrophilic-hydrophobic graft polymer with controllable main and side chain lengths | |
JP2010209340A (en) | Method for producing multi-branched polymer | |
CN107849183B (en) | Vinyl ether-vinyl ester copolymers | |
Ding et al. | PDMAEMA-b-PPOA-b-PDMAEMA double-bond-containing amphiphilic triblock copolymer: synthesis, characterization, and pH-responsive self-assembly | |
CN106046221B (en) | The catalyst and polymerization of a kind of reversible-suspend mode free radical polymerization | |
Karagoz et al. | Functionalization of poly (divinylbenzene) microspheres by combination of hydrobromination and click chemistry processes: a model study | |
Ding et al. | ATRP synthesis of polyallene-based amphiphilic triblock copolymer | |
CN101323570A (en) | Functional acrylate monomer containing atom transfer radical polymerization initiating group, synthesis method and use thereof | |
CN102604011A (en) | Amphiphilic multi-arm star-like polymer and preparation method thereof | |
JP2022553490A (en) | Degradable polymer material | |
CN102212166A (en) | Novel method for performing copolymerization reaction of dicyclopentadiene and maleic anhydride | |
CN114195962B (en) | Amphiphilic fluorine-containing block polymer and preparation method and application thereof | |
CN104334593A (en) | Polymer, method for preparing same, and composition and film comprising same | |
US12065519B2 (en) | Synthesis of polymer under conditions of enhanced catalyzed radical termination | |
JP2003026724A (en) | Method for producing polymer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Jiangsu Guoli Chemical Technology Co., Ltd. Assignor: Jiangnan University Contract fulfillment period: 2009.3.15 to 2014.3.14 contract change Contract record no.: 2009320000657 Denomination of invention: Process for preparing hydrophilic-hydrophobic graft polymer with controllable main and side chain length Granted publication date: 20080917 License type: Exclusive license Record date: 2009.4.22 |
|
LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.3.15 TO 2014.3.14; CHANGE OF CONTRACT Name of requester: JIANGSU GUOLI CHEMICAL SCIENCE CO., LTD. Effective date: 20090422 |
|
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080917 Termination date: 20150417 |
|
EXPY | Termination of patent right or utility model |