CN1603349A - Method for polymerization of alpha, beta-unsaturated carbonyl and nitrile monomer - Google Patents
Method for polymerization of alpha, beta-unsaturated carbonyl and nitrile monomer Download PDFInfo
- Publication number
- CN1603349A CN1603349A CN 03134702 CN03134702A CN1603349A CN 1603349 A CN1603349 A CN 1603349A CN 03134702 CN03134702 CN 03134702 CN 03134702 A CN03134702 A CN 03134702A CN 1603349 A CN1603349 A CN 1603349A
- Authority
- CN
- China
- Prior art keywords
- cuprous
- organic
- polymerization
- lithium
- copper
- 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.)
- Granted
Links
Landscapes
- Polymerization Catalysts (AREA)
Abstract
This invention puts forward a polymerization method of alpha,beta-unsaturation carbonyl and nitrile grouping monomer. Initiator system is consisted by organic lithium and monovalence cupric salt and monovalence organic copper compound or monovalence cupric salt and monovalence copper organic complex, then polymerization reaction is initiated proceeded byalpha,beta-unsaturation carbonyl and nitrile grouping monomer. Polymerization side reaction is few when initiator is reacted with alpha,beta-unsaturation carbonyl and nitrile grouping monomer, so the polymerization can proceed under room temperature and can be used conveniently to synthesis of polarity- nonpolarity block copolymer. Quick polymerization reaction and high efficiency of initiation and yield are features.
Description
Technical field
The present invention relates to a kind of anionic polymerisation process, particularly cause α, the monomeric anionic polymerisation process of beta-unsaturated carbonyl and itrile group with organo-metallic.
Background technology
Representative α, beta-unsaturated carbonyl and itrile group monomer mainly comprise methyl acrylic ester, esters of acrylic acid and vinyl cyanide, methacrylonitrile etc.They can both carry out anionoid polymerization and radical polymerization, not only can controlling polymers relative molecular mass and distribution and microtexture by living anion polymerization, and can with other non-polar monomer, as the synthetic multiple amphiphilic segmented copolymer of copolymerization such as vinylbenzene, divinyl.Traditional, the initiator of organic alkali metal compound and Grignard reagent is generally adopted in the monomeric anionoid polymerization of (methyl) acrylate isopolarity.Main drawback shows that organic alkali metal compound and Grignard reagent are is the carbanion spike of gegenion with basic metal and alkaline-earth metal, and groups such as carbonyl and itrile group are had the intensive nucleation, and the polymerization process side reaction is serious.Have only the spike of reduction activity, reduce polymerization temperature and could realize living polymerization.Many researchists have carried out big quantity research at initiator system.As US.4056580, basic metal isobutyrate class and additive composition initiator system that alpha-position replaces were disclosed in 1977, wherein additive has tert.-butoxy an alkali metal salt, lithium chloride, σ/μ-type binary part (Ligand) (as LiO (CH
2CH
2O)
nCH
3) etc.Because part has increased the volume of spike end, thereby reduce or avoid " inventing a charge against " termination reaction of spike.But still need in low temperature polymerization.Polymer Preprints, 1994,35 (2), 599 adopt BuLi/R
3Al is an initiator system.It can make methyl methacrylate (MMA) or butyl methacrylate (BuMA)-5~-10 ℃ of polymerizations in toluene, and transformation efficiency reaches 100%, and relative molecular mass distributes less than 1.2, but efficiency of initiation is lower.Macromolecules, 1995,28,7315-317 has reported 1,1-phenylbenzene hexyl lithium DPHLi and Lewis base (as tetramethyl-ethylene base diamines TMEDA).Can make polymerization temperature be increased to-40 ℃ in THF, experiment shows that the relative molecular mass of product is controlled, and the relative molecular mass distribution coefficient is less than 1.2.
Above-mentioned initiator system is to be gegenion with the organic alkali metal mostly, has added different parts.Therefore, be referred to as compatibility anionoid polymerization (Ligand Anionic Polymerization).Though present above-mentioned research has obtained remarkable progress, but still exists polymerization temperature lower, or the not high shortcoming of efficiency of initiation.
Summary of the invention
The technical problem that the present invention solves: in order to overcome organic alkali metal or alkaline earth metal compound to α, the attack of carbonyl and itrile group in beta-unsaturated carbonyl and the itrile group compound, and problem such as the polymerization temperature that existing initiator system exists is lower, efficiency of initiation is not high, the present invention proposes a kind of anionic solution polymerization method, initiator and α, polymerization side reactions is few when beta-unsaturated carbonyl and the reaction of itrile group compound, polymerization can be carried out in room temperature, and have higher efficiency of initiation.
Main technical schemes: at α, in beta-unsaturated carbonyl and the itrile group monomer anionic solution polymerization system, organic complex and organolithium with cuprous salt, monovalence organocopper compound or cuprous salt, monovalence organic copper are formed initiator system, cause α, beta-unsaturated carbonyl and itrile group polymerisable monomer carry out anionic polymerization.Wherein cuprous salt mainly comprises cuprous chloride, cuprous bromide, cuprous iodide, cuprous cyanide or cuprous rhodanide etc.; Monovalence organocopper compound structure bromine formula is RCu, and R is alkyl, alkoxyl group, alkynyl in the formula; Cuprous salt or monovalence organic copper organic complex chemical structural formula are XCuA, RCuA, and X is in the formula: chlorion, bromide anion, iodide ion, cyano group, thiocyanogen, R is: alkyl, alkoxyl group, alkynyl, A are the organic compound that has elements such as S, N, P.The mole number of initiator system copper is 1% to 100% of a lithium, and concrete additional proportion is formed the initiator system composition with organolithium respectively according to cuprous salt, monovalence organocopper compound or their organic complex and changed to determine.Mole such as ligand mole number and organic copper or excessive below 50%.
In the above-mentioned anionic solution polymerization system, polymer solvent is dimethyl formamide (DMF), methyl-sulphoxide, tetrahydrofuran (THF) (THF), ether, methyl-phenoxide, toluene, benzene, or the mixed solvent of these solvents and alkane composition, polymerisable monomer is methacrylic ester, acrylate, vinyl cyanide, methacrylic nitrile;
Above-mentioned organolithium comprises: lithium alkylide, phenyl lithium, benzyl lithium and allyl group lithium etc.
Effect of the present invention: 1, polymerization side reactions is few, and organic copper reagent and α are 1 when beta-unsaturated carbonyl and the reaction of itrile group compound, the 4-addition, and product keeps carbonyl or itrile group group, effectively eliminates or the minimizing side reaction.2, owing to reduced side reaction, therefore can increase substantially polymerization temperature, polymerization can be carried out at-20 to 30 ℃.3,, therefore can be advantageously used in the synthetic of polarity-non-polar blocks multipolymer because the organic copper initiator can pass through original position metal transfer prepared in reaction.4, experiment shows that this polymerization process has easy realization, and polymerization time is short, and monomer conversion reaches advantage such as 99%.
Embodiment:
In the anionic solution polymerization system, polymer solvent is the mixed solvent that dimethyl formamide (DMF), methyl-sulphoxide, tetrahydrofuran (THF) (THF), ether, methyl-phenoxide, toluene, benzene or these solvents and alkane are formed, wherein alkane is mainly hexanaphthene, hexane etc., contain below 80% (volume), be preferably (volume) below 50%; Polymerisable monomer is methacrylic ester, acrylate, vinyl cyanide, methacrylic nitrile; Initiator is the initiator system that organolithium and cuprous salt, monovalence organocopper compound or their organic complex are formed, and wherein cuprous salt mainly is cuprous chloride, cuprous bromide, cuprous iodide, cuprous cyanide or cuprous rhodanide etc.; The monovalence organocopper compound mainly is alkyl copper, alkoxyl group copper etc.; The cuprous salt organic complex is the complex compound that cuprous salt or organic copper and alkyl or aryl thioether, alkyl or aryl phosphorus, alkyl or aryl boron are formed, as: alkyl nitrogen, the positive butyl ester of phosphorous acid, trialkyl phosphorus, triaryl phosphorus etc.Organolithium comprises: lithium alkylide, phenyl lithium, benzyl lithium and allyl group lithium etc.The polymerisable monomer structure has methacrylic ester, acrylate, 2-butylene acid esters, vinyl cyanide and methacrylonitrile etc.Under the situation of starvation, moisture, carry out polymerization in nitrogen atmosphere.Monomer concentration is below 20%, is preferably below 10%, and polymerization temperature a wider range, from-78 to 70 ℃ of polymerizables all can be-20 to 30 ℃ of polymerizations.
The preparation of initiator of the present invention has following embodiment with the initiator system that organolithium is formed respectively according to cuprous salt, monovalence organocopper compound or their organic complex:
The preparation of cuprous salt and organic lithium initiator system is in solvent system, adds the cuprous salt below 50% of organolithium mole number, is stirring the adding organolithium compound below 0 ℃ then;
Cuprous salt complex compound and organic lithium initiator at first by cuprous salt and complexing agent reaction, generate the cuprous salt organic complex, are stirring the adding organolithium compound below 0 ℃ then, and wherein the mole number of copper is less than the organolithium mole number;
The preparation of organic copper and organic lithium initiator is at first to prepare organic copper by organolithium and cuprous chloride, cuprous bromide or cuprous iodide, adds with mole such as copper then or excessive basic lithium is arranged.
The following examples are for further specifying method of the present invention.
Embodiment 1
The 100ml three-necked bottle charges into nitrogen through vacuum bakeout, adds the 50ml tetrahydrofuran (THF) with syringe, and accurately weighing 0.0495g cuprous chloride adds 1.0mol/L concentration n-Butyl Lithium 1.0ml then, reacts 2min to 30min at 0 ℃.20 ℃ add methyl methacrylate 5g, polymerization time 20 minutes.With gel liquid chromatography (GPC), nuclear-magnetism means of testing such as (NMR) polymerization is characterized after removing solvent.Polymericular weight is 13000, is distributed as 1.1 to 1.6.
Embodiment 2
The 100ml three-necked bottle charges into nitrogen through vacuum bakeout, adds the 50ml dimethyl formamide with syringe, and accurately weighing 0.0495g cuprous chloride adds 1.0mol/L concentration phenyl lithium 1.0ml then, reacts 2min to 30min at-20 ℃.-20 ℃ add methyl methacrylate 5g, polymerization time 40 minutes.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 13000, is distributed as 1.1 to 1.6.
Embodiment 3
The 100ml three-necked bottle charges into nitrogen through vacuum bakeout, adds 50ml toluene with syringe, and accurately weighing 0.0495g cuprous iodide adds 1.0mol/L concentration n-Butyl Lithium 1.0ml then, reacts 2min to 30min at-78 ℃.-78 ℃ add methyl methacrylate 5g, polymerization time 60 minutes.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 10000, is distributed as 1.1 to 2.0.
Embodiment 4
The 100ml three-necked bottle charges into nitrogen through vacuum bakeout, adds 50ml ether and 0.01g cuprous chloride with syringe, adds 1.0mol/L concentration n-Butyl Lithium 1.0ml then, reacts half an hour at 0 ℃.Add methyl methacrylate 5g, polymerization time 20 minutes at 20 ℃.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 30000, is distributed as 1.1 to 1.6.
Embodiment 5
The 100ml three-necked bottle charges into nitrogen through vacuum bakeout, adds 50ml tetrahydrofuran (THF), 1mmol tri-isobutyl-boron and 0.099g cuprous bromide with syringe, adds 1.0mol/L concentration n-Butyl Lithium 1.0ml then, and concentration is reacted half an hour at 0 ℃.Add methyl methacrylate 5g, polymerization time 20 minutes at 20 ℃.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 15000, is distributed as 1.1 to 1.6.
Embodiment 6
At first in ether, prepare alkyl copper, remove by filter lithium iodide by cupric iodide and n-Butyl Lithium.In the three-necked bottle of 100ml, put into the 50ml tetrahydrofuran (THF), the alkyl copper 2ml that adds 1.0mol/L concentration n-Butyl Lithium 1.0ml and 0.5mol/L concentration then reacts half an hour at 0 ℃.Add methyl methacrylate 5g, polymerization time 20 minutes at 20 ℃.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 12000, is distributed as 1.1 to 1.6.
Embodiment 7
Press embodiment 6 preparation alkyl copper, remove by filter lithium iodide and add and the equimolar tri-isobutyl-boron of alkyl copper generation RCuB (s-Bu)
3In the three-necked bottle of 100ml, put into the 50ml tetrahydrofuran (THF), add the RCuB (s-Bu) of 1.0mol/L concentration n-Butyl Lithium 1.0ml and 0.5mol/L concentration then
3Solution 2ml reacts half an hour at 0 ℃.Add methyl methacrylate 5g, polymerization time 20 minutes at 20 ℃.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 12000, is distributed as 1.1 to 1.6.
Embodiment 8
In the three-necked bottle of 100ml, put into 50ml tetrahydrofuran (THF)/hexanaphthene mixed solution, triisobutyl phosphorus and 0.099g cuprous chloride add 1.0mol/L concentration n-Butyl Lithium 1.0ml then, react half an hour at 0 ℃.Add methyl methacrylate 5g, polymerization time 20 minutes at 20 ℃.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 12000, is distributed as 1.1 to 1.6.
Embodiment 9
In the three-necked bottle of 100ml, put into the 50ml tetrahydrofuran (THF).In this solvent, make Virahol and n-Butyl Lithium reaction with same mole, add cuprous chloride then, generate alkoxyl group copper RCu.Add 1.0mol/L concentration n-Butyl Lithium 1.0ml at last, react half an hour at 0 ℃.Add methyl methacrylate 5g, polymerization time 20 minutes at 20 ℃.With means of testing such as GPC, NMR polymerization is characterized after removing solvent.Polymericular weight is 12000, is distributed as 1.1 to 1.6.
Experiment 10
The 100ml three-necked bottle charges into nitrogen through vacuum bakeout, adds the 50ml dimethyl formamide with syringe, and accurately weighing 0.0495g cuprous chloride adds 1.0mol/L concentration phenyl lithium 1.0ml then, reacts 2min to 30min at-20 ℃.-20 ℃ add vinyl cyanide 5g, and polymerization time 40 minutes obtains white or slightly yellowy polymer powder.
Claims (6)
1, a kind of α, the monomeric polymerization process of beta-unsaturated carbonyl and itrile group, at α, in beta-unsaturated carbonyl and the itrile group polymerizable monomer solution system, the initiator of forming with organo-metallic carries out anionoid polymerization, it is characterized in that: the organo-metallic initiator is formed initiator system by metal cuprous salt, monovalence organocopper compound, cuprous salt or monovalence organic copper organic complex and organolithium, and wherein cuprous salt mainly comprises cuprous chloride, cuprous bromide, cuprous iodide, cuprous cyanide or cuprous rhodanide; Monovalence organocopper compound structural formula is RCu, and R is alkyl, alkoxyl group, alkynyl in the formula; Cuprous salt or monovalence organic copper organic complex chemical structural formula are XCuA, RCuA, and X is in the formula: chlorine, bromine, iodine and cyano group and thiocyanogen, and R is: alkyl, alkoxyl group, alkynyl, A are the organic compound that has elements such as S, N, P; The mole number of initiator system copper is 1% to 100% of a lithium, mole such as ligand mole number and organic copper or excessive below 50%.
2, according to the polymerization process of claim 1, it is characterized in that: α, in beta-unsaturated carbonyl and the itrile group polymerizable monomer solution system, polymer solvent is dimethyl formamide, methyl-sulphoxide, tetrahydrofuran (THF), ether, methyl-phenoxide, toluene, benzene, or the mixed solvent of these solvents and alkane composition; Polymerisable monomer is methacrylic ester, acrylate, vinyl cyanide, methacrylic nitrile.
3, according to the polymerization process of claim 1, it is characterized in that: the preparation of cuprous salt and organic lithium initiator system is in solvent system, adds the cuprous salt below 50% of organolithium mole number, is stirring the adding organolithium compound below 0 ℃ then.
4, according to the polymerization process of claim 1, it is characterized in that: cuprous salt complex compound and organic lithium initiator are at first by cuprous salt and complexing agent reaction, generate the cuprous salt organic complex, stirring the adding organolithium compound below 0 ℃ then, wherein the mole number of copper is less than the organolithium mole number.
5, according to the polymerization process of claim 1, it is characterized in that: the preparation of organic copper and organic lithium initiator is at first to prepare organic copper by organolithium and cuprous chloride, cuprous bromide or cuprous iodide, then mole or excessive organolithiums such as adding and copper.
6, according to the polymerization process of claim 1, it is characterized in that: described organolithium comprises: lithium alkylide, phenyl lithium, benzyl lithium and allyl group lithium.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03134702 CN1241960C (en) | 2003-09-29 | 2003-09-29 | Method for polymerization of alpha, beta-unsaturated carbonyl and nitrile monomer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 03134702 CN1241960C (en) | 2003-09-29 | 2003-09-29 | Method for polymerization of alpha, beta-unsaturated carbonyl and nitrile monomer |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1603349A true CN1603349A (en) | 2005-04-06 |
CN1241960C CN1241960C (en) | 2006-02-15 |
Family
ID=34659078
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 03134702 Expired - Fee Related CN1241960C (en) | 2003-09-29 | 2003-09-29 | Method for polymerization of alpha, beta-unsaturated carbonyl and nitrile monomer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1241960C (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100371356C (en) * | 2006-06-23 | 2008-02-27 | 北京化工大学 | Negative charged ion polymerization method of 2,2,2-Trifluorethylmethyl acrylate |
CN105101935A (en) * | 2013-03-28 | 2015-11-25 | 可乐丽则武齿科株式会社 | Curable composition |
-
2003
- 2003-09-29 CN CN 03134702 patent/CN1241960C/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100371356C (en) * | 2006-06-23 | 2008-02-27 | 北京化工大学 | Negative charged ion polymerization method of 2,2,2-Trifluorethylmethyl acrylate |
CN105101935A (en) * | 2013-03-28 | 2015-11-25 | 可乐丽则武齿科株式会社 | Curable composition |
US9889070B2 (en) | 2013-03-28 | 2018-02-13 | Kuraray Noritake Dental Inc. | Curable composition |
CN105101935B (en) * | 2013-03-28 | 2018-02-23 | 可乐丽则武齿科株式会社 | Solidification compound |
Also Published As
Publication number | Publication date |
---|---|
CN1241960C (en) | 2006-02-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4656233A (en) | "Living" polymers and chain transfer-regulated polymerization process | |
JP2009509003A5 (en) | ||
US4767824A (en) | Process for polymerizing acrylic monomers and possibly non-acrylic co-monomers | |
JP2009509014A5 (en) | ||
Furukawa et al. | Catalytic reactivity and stereospecificity of organometallic compounds in olefin polymerization | |
US9181374B2 (en) | Process for preparing branched polymer | |
CN109251260A (en) | Active polymerization system based on phosphine base catalysis synthesizing super high molecular weight polymer | |
WO1997033923A1 (en) | Process for the preparation of vinylic polymers, polymerization initiator for vinylic monomers, and styrene resin composition | |
CN111320717A (en) | Method for catalyzing vinyl monomer polymerization by using hindered Lewis acid-base pair based on binuclear aluminum Lewis acid | |
CN1241960C (en) | Method for polymerization of alpha, beta-unsaturated carbonyl and nitrile monomer | |
JP5805006B2 (en) | Copolymer of vinyl ester and vinyl ether, and method for producing the same | |
JP4767552B2 (en) | Phenolic star polymer | |
JP3516812B2 (en) | Method for producing acrylic block copolymer | |
CN1222532A (en) | Catalytic complexes based on lanthanides for (co) polymerization of conjugated dienes | |
CN1148053A (en) | Multi-functional group organic alkali metal initiator, and synthesis method therefor | |
CN110799553B (en) | Process for producing polymers | |
CN1098868C (en) | Catalyst system for preparation of high crystalline polypropylene and making method thereof | |
JP2001508090A (en) | Method for producing polyalkyl (meth) acrylate | |
CN1206248C (en) | Method of raising the stability of isobutene polymer slurry | |
CA1296129C (en) | Polymerization of acrylic derivatives | |
JPS63202607A (en) | Polymerization method | |
CN1342718A (en) | Rare-earth catalysis process for polymerizing biolefine | |
CN1160386C (en) | Living polymerisation process | |
AU737973B2 (en) | Process for preparing polymer by using copper compound | |
JPH0822881B2 (en) | Method for producing conjugated diene-based polymers |
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 | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |