CN103641938A - Initiator for alkene monomer polymerization reaction - Google Patents

Initiator for alkene monomer polymerization reaction Download PDF

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CN103641938A
CN103641938A CN201310726322.XA CN201310726322A CN103641938A CN 103641938 A CN103641938 A CN 103641938A CN 201310726322 A CN201310726322 A CN 201310726322A CN 103641938 A CN103641938 A CN 103641938A
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polymerization
initiator
compound
vinyl monomer
butyronitrile
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CN103641938B (en
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程斌
鲍彦广
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Beijing University of Chemical Technology
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Beijing University of Chemical Technology
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Abstract

The invention discloses an initiator for alkene monomer polymerization reaction, and belongs to the technical field of imitators. A compound 2,3-diphenyl butyronitrile is applied to initiating polymerization of alkene monomers such as acrylic ester, metacrylic acid ester and styrene, the polymerization method mainly refers to bulk polymerization or solution polymerization, and the initiated polymerization temperature is 70-130 DEG C. The compound 2,3-diphenyl butyronitrile can be dissolved by the solvent adopted in solution polymerization. By adopting the initiator, a polymerization initiator system is expanded, and polymers with high molecular weight are easily obtained.

Description

A kind of initiator that can be used for vinyl monomer polyreaction
Technical field
The present invention relates to a kind of new purposes of compound, especially 2, the new purposes of 3-phenylbenzene butyronitrile, can be used as initiator for causing the polymerization of vinyl monomer, belongs to initiator technical field.
Background technology
Macromolecular compound is generally made by initiator system trigger monomer generation polymerization.Initiator system plays indispensable effect in macromolecular compound preparation process, makes a general survey of polymer science developing history, and initiator system evolution history is exactly the development history of polymer science.Existing high molecular polymerization initiator system divides five large classes, is respectively free radical initiator system, cationic initiator system, anionic initiator system, polycoordination initiator system and group transfer polymerization initiator system.
Polycoordination initiator system is very successful initiator system, and what several influential plastics, rubber clone adopted is polycoordination initiator system.But polycoordination initiator system is had relatively high expectations to polymerization environment, and initiator system preparation is complicated, higher to transportation, storage request.
Anionic initiation system is prepared complexity equally, to transportation, storage request is higher, very high to polymerization environmental requirement.And anionic initiation system use range is very narrow, successfully Industrial products only have several.
Positively charged ion initiator system range of application is narrower, and group transfer polymerization does not also have practical application.
In macromolecular compound preparation, free radical initiator system is most widely used general.Mainly be divided into two classes: thermal initiation system, redox system.On the molecular structure of radical initiator, there is weak bond, easily resolve into free radical.Thermal initiation system is single compound, by heating, the weak bond in compound is ruptured, and produces free radical and initiated polymerization mainly divides azo-compound and superoxide two classes.Thermal initiation system, easy to use, be main initiator system prepared by macromolecular compound.Redox system is two components, and a kind of is superoxide, and a kind of is reductive agent.Use range is narrower compared with thermal initiation system.
The relative cationic initiator system of free radical initiator system, anionic initiator system, polycoordination initiator system is many easily, and major advantage is as follows: 1, component is single, and preparation is simple; 2, easy to use; 3, storage, movement requirement are lower.But, because it mostly is azo, peroxide compound, there is the risk of blast.Also a lot of inconvenience of having given use, storage and travelling belt.
Compound 2, the preparation of 3-phenylbenzene butyronitrile is by reference to pertinent literature [Additional and substitution reactions of nitrile-stabilized carbanions, By Arseniyadis, Simeon; Kyler, Keithsi, Watt, Davids; From Organic Reactions (Hoboken, NJ, United States) No pp.given; 1984] preparation.
Summary of the invention
The present invention relates to the compound in a kind of organic synthesis field, the polymerization of the vinyl monomer such as this compound can Methyl Methacrylate, ethyl propenoate, vinylbenzene.Because being solid-state under its normal temperature, thus be convenient to storage, transportation, and preparation method is simple, cost is lower, when possessing the general advantage of free radical initiator system, has also overcome the part defect of conventional free radical initiator, has expanded initiator system.
The initiator the present invention relates to, is compound 2,3-phenylbenzene butyronitrile, and its structural formula is
Figure BDA0000445780970000021
The preparation method of the compound that the present invention mentions (I), by the preparation of improving one's methods, concrete synthetic method comprises the steps:
By phase-transfer catalyst TEBAC and highly basic NaOH(or KOH) be dissolved in distilled water, under agitation condition, slowly drip the mixed solution of chlorinated benzene ethane and two kinds of raw materials of benzyl cyanide, after 50~60 ℃ of reaction 8~10h, add the static termination reaction of ice-water bath or normal temperature, with dichloromethane solvent, extract afterwards, extract organic layer, then use anhydrous MgSO 4dry, solvent evaporated, column chromatography for separation is purified, and gets final product to obtain compound (I).Reaction equation is as follows:
Figure BDA0000445780970000031
The compound the present invention relates to can be used for causing the polymerization of vinyl monomer, especially (methyl) esters of acrylic acid or cinnamic polymerization, as acrylate, methacrylic ester, vinylbenzene etc., the polymerization process relating to is mainly mass polymerization or solution polymerization, and initiated polymerization temperature is 70-130 ℃.The solvent adopting during solution polymerization can dissolved compound (I).
Compound of the present invention is as initiator; substantially the same with conventional initiator usage; as nitrogen protection etc.; and the present invention has use and storage security; simple to operate, synthetic method is simple, and cost is lower; and the advantage of the polymkeric substance that the molecular weight that is easy to get is higher, has expanded polymerization initiator system.
Accompanying drawing explanation
Fig. 1 is the compound 2 of preparation, 3-phenylbenzene butyronitrile 1h NMR spectrogram.
Embodiment
Below in conjunction with specific embodiment, further set forth the present invention.Should be understood that these embodiment are only not used in and limit the scope of the invention for the present invention is described.In addition, after having read the content of the present invention's instruction, those skilled in the art can make various changes or modifications the present invention, and these equivalent form of values fall within the application's appended claims limited range equally.
Initiator A: the preparation of 2,3-phenylbenzene butyronitrile (structural formula 1):
By consisting of phase-transferring agent benzyl triethyl ammonium bromide (TEBAC) (4.587g, 0.02mol), NaOH solid (4g left and right, 0.1mol) join in 10ml distilled water, under magnetic agitation, chlorinated benzene ethane (2.81g, 0.02mol) and benzyl cyanide (2.34g, 0.02mol) are slowly added drop-wise in reaction system, after 50~60 ℃ of reaction 8~10h, add the static termination reaction of ice-water bath or normal temperature.With dichloromethane solvent extraction, extract organic layer, then use anhydrous MgSO afterwards 4dry, solvent evaporated, column chromatography for separation is purified, and gets final product to obtain compd A.
Embodiment 1
1g methyl methacrylate monomer, 0.0222g initiator A and 2ml toluene solvant are joined in polymerizing pipe, mix rear good seal, under liquid nitrogen freezing or cold condition, vacuumize-inflated with nitrogen 5 times repeatedly.Polymerizing pipe is put into after reacting 10h under 80 ℃ of oil baths and takes out polymerizing pipe, termination reaction under low temperature.Then with sherwood oil or methanol/water=1:1 solvent deposition polymkeric substance, 50 ℃ of vacuum drying ovens its transformation efficiency that dries to constant weight is 32.01%, records polymkeric substance number-average molecular weight (M n)=90714, molecular weight distribution width (PDI)=1.74.The blank group that does not add initiator A under the same terms does not have polymerization completely.
Embodiment 2
1g methyl methacrylate monomer, 0.0222g initiator A and 2ml toluene solvant are joined in polymerizing pipe, mix rear good seal, under liquid nitrogen freezing or cold condition, vacuumize-inflated with nitrogen 5 times repeatedly.Polymerizing pipe is put into after reacting 10h under 85 ℃ of oil baths and takes out polymerizing pipe, termination reaction under low temperature.Then with sherwood oil or methanol/water=1:1 solvent deposition polymkeric substance, 50 ℃ of vacuum drying ovens its transformation efficiency that dries to constant weight is 52.44%, records polymkeric substance number-average molecular weight (M n)=91531, molecular weight distribution width (PDI)=1.77.Although and under the same terms, do not add blank group of slightly polymerization of initiator A, polymerization amount is considerably less.
Embodiment 3
About 1.04g styrene monomer and 0.0222g initiator A are joined in polymerizing pipe, mix rear good seal, under liquid nitrogen freezing or cold condition, vacuumize-inflated with nitrogen 5 times repeatedly.Polymerizing pipe is put into after reacting 3h under 120 ℃ of oil baths and takes out polymerizing pipe, termination reaction under low temperature.Then with sherwood oil or methanol/water=1:1 solvent deposition polymkeric substance, 50 ℃ of vacuum drying ovens its transformation efficiency that dries to constant weight is 52.20%, records polymkeric substance M n=153042, PDI=1.78.
Embodiment 4
About 1.04g styrene monomer and 0.0222g initiator A are joined in polymerizing pipe, mix rear good seal, under liquid nitrogen freezing or cold condition, vacuumize-inflated with nitrogen 5 times repeatedly.Polymerizing pipe is put into after reacting 3h under 130 ℃ of oil baths and takes out polymerizing pipe, termination reaction under low temperature.Then with sherwood oil or methanol/water=1:1 solvent deposition polymkeric substance, 50 ℃ of vacuum drying ovens its transformation efficiency that dries to constant weight is 62.73%, records polymkeric substance M n=122334, PDI=1.85.

Claims (5)

1. compound 2, and 3-phenylbenzene butyronitrile is for causing the polymerization of vinyl monomer.
2. according to the compound of claim 12,3-phenylbenzene butyronitrile is used for causing the polymerization of vinyl monomer, it is characterized in that, polymerization process is mainly mass polymerization or solution polymerization.
3. according to the compound of claim 12,3-phenylbenzene butyronitrile, for causing the polymerization of vinyl monomer, is characterized in that, compound 2, and 3-phenylbenzene butyronitrile is for causing the polymerization of vinyl monomer, and initiated polymerization temperature is 70-130 ℃.
4. according to the compound of claim 22,3-phenylbenzene butyronitrile, for causing the polymerization of vinyl monomer, is characterized in that, the solvent adopting during solution polymerization can dissolved compound 2,3-phenylbenzene butyronitrile.
5. according to arbitrary compound 2 of claim 1-4,3-phenylbenzene butyronitrile is used for causing the polymerization of vinyl monomer, it is characterized in that, described vinyl monomer is acrylate, methacrylic ester or vinylbenzene.
CN201310726322.XA 2013-12-25 2013-12-25 A kind of initiator that can be used for vinyl monomer polyreaction Expired - Fee Related CN103641938B (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105348564A (en) * 2015-10-30 2016-02-24 成都新柯力化工科技有限公司 Preparation method of inorganic powder specially used for low-density composite ivory boards
CN108059690A (en) * 2017-12-20 2018-05-22 西安理工大学 Initiation system containing alkyl trifluoroborate and its method for triggering monomer polymerization

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102675491A (en) * 2012-01-10 2012-09-19 北京化工大学 Novel initiating system, and preparation method and application thereof

Patent Citations (1)

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Publication number Priority date Publication date Assignee Title
CN102675491A (en) * 2012-01-10 2012-09-19 北京化工大学 Novel initiating system, and preparation method and application thereof

Non-Patent Citations (4)

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Title
TAKAYUKI OTSU ET AL: "Role of Initiator-Transfer Agent-Terminator (Iniferter) in Radical Polymerizations: Polymer Design by Organic Disulfides as Iniferters", 《MAKROMOL. CHEM., RPPID COMRNUN》 *
TAKAYUKI OTSU: "Iniferter Concept and Living Radical Polymerization", 《JOURNAL OF POLYMER SCIENCE: PART A: POLYMER CHEMISTRY》 *
刘洪波: "位阻效应对引发- 转移- 终止剂 引发和控制活性自由基聚合的影响", 《顺德职业技术学院学报》 *
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105348564A (en) * 2015-10-30 2016-02-24 成都新柯力化工科技有限公司 Preparation method of inorganic powder specially used for low-density composite ivory boards
CN105348564B (en) * 2015-10-30 2018-06-26 太原理工大学 A kind of compound art post paperboard special inorganic raw powder's production technology of low-density
CN108059690A (en) * 2017-12-20 2018-05-22 西安理工大学 Initiation system containing alkyl trifluoroborate and its method for triggering monomer polymerization
CN108059690B (en) * 2017-12-20 2020-08-18 西安理工大学 Initiation system containing alkyl trifluoroborate and method for initiating monomer polymerization by using initiation system

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