US20160297755A1 - Radical polymerization initiator and method for producing polymers - Google Patents

Radical polymerization initiator and method for producing polymers Download PDF

Info

Publication number
US20160297755A1
US20160297755A1 US15/038,579 US201415038579A US2016297755A1 US 20160297755 A1 US20160297755 A1 US 20160297755A1 US 201415038579 A US201415038579 A US 201415038579A US 2016297755 A1 US2016297755 A1 US 2016297755A1
Authority
US
United States
Prior art keywords
group
substituted
unsubstituted
polymer
producing
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.)
Abandoned
Application number
US15/038,579
Other languages
English (en)
Inventor
Fumiaki Bando
Shigeru Yamago
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zeon Corp
Kyoto University NUC
Original Assignee
Zeon Corp
Kyoto University NUC
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Zeon Corp, Kyoto University NUC filed Critical Zeon Corp
Assigned to KYOTO UNIVERSITY, ZEON CORPORATION reassignment KYOTO UNIVERSITY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BANDO, FUMIAKI, YAMAGO, SHIGERU
Publication of US20160297755A1 publication Critical patent/US20160297755A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C395/00—Compounds containing tellurium
    • 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
    • C08F112/00—Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F112/02—Monomers containing only one unsaturated aliphatic radical
    • C08F112/04—Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F112/06—Hydrocarbons
    • C08F112/08—Styrene
    • 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
    • C08F12/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F12/02—Monomers containing only one unsaturated aliphatic radical
    • C08F12/04—Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F12/06—Hydrocarbons
    • C08F12/08—Styrene
    • 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
    • C08F120/00—Homopolymers 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
    • C08F120/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F120/10—Esters
    • C08F120/34—Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate
    • 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
    • C08F2/00—Processes of polymerisation
    • C08F2/46—Polymerisation initiated by wave energy or particle radiation
    • C08F2/48—Polymerisation initiated by wave energy or particle radiation by ultraviolet or visible light
    • 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
    • C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02—Monomers containing only one unsaturated aliphatic radical
    • C08F212/04—Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F212/06—Hydrocarbons
    • C08F212/08—Styrene
    • 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
    • C08F220/10—Esters
    • C08F220/12—Esters of monohydric alcohols or phenols
    • 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
    • C08F220/10—Esters
    • C08F220/12—Esters of monohydric alcohols or phenols
    • C08F220/14—Methyl esters, e.g. methyl (meth)acrylate
    • 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
    • C08F236/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
    • C08F236/02—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
    • C08F236/04—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated
    • C08F236/08—Isoprene
    • 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
    • C08F236/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
    • C08F236/02—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
    • C08F236/04—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated
    • C08F236/12—Copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated with nitriles
    • 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
    • C08F299/00—Macromolecular compounds obtained by interreacting polymers involving only carbon-to-carbon unsaturated bond reactions, in the absence of non-macromolecular monomers
    • 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
    • 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
    • C08F4/04—Azo-compounds

Definitions

  • the present invention relates to a radical polymerization initiator that is useful for producing a polymer that includes a double bond at the molecular terminal, and a method for producing a polymer that utilizes the radical polymerization initiator.
  • a polymer that includes a double bond at the molecular terminal is used as a macromonomer when producing a polymer that has a branched structure (e.g., graft polymer or star-shaped polymer).
  • Patent Literature 1 discloses a method for producing a polymer having a branched structure wherein a macromonomer is polymerized, the macromonomer including a group that includes a polymerizable carbon-carbon double bond at the molecular terminal.
  • Patent Literature 1 discloses a method for producing a macromonomer wherein a vinyl-based monomer is polymerized using an atom transfer radical polymerization method that utilizes a polymerization initiator (e.g., organic halide) and a catalyst (e.g., transition metal complex) to obtain a vinyl-based polymer that includes a terminal halogen group, and the terminal halogen group is substituted with a compound that includes a double bond, for example.
  • a polymerization initiator e.g., organic halide
  • a catalyst e.g., transition metal complex
  • Patent Literature 1 When using the method disclosed in Patent Literature 1 wherein a functional group (e.g., halogen group) situated at the molecular terminal is substituted with a group that includes a carbon-carbon double bond, it is necessary to effect a functional group substitution reaction. Therefore, a method that introduces a carbon-carbon double bond into the polymerization-initiation terminal using a polymerization initiator that includes a carbon-carbon double bond has been studied in order to more easily obtain a macromonomer. Examples of such a method include an atom transfer radical polymerization method that utilizes an allyl halide as a polymerization initiator (see Non-Patent Literature 1).
  • a functional group e.g., halogen group
  • the type of vinyl-based monomer that can be applied to the atom transfer radical polymerization method that utilizes an allyl halide as a polymerization initiator is limited. Moreover, it may be difficult to control the polymerization reaction, or the polymerization reaction may not proceed depending on the type of vinyl-based monomer.
  • a radical polymerization initiator that includes a carbon-carbon double bond and can be applied to a wide variety of radically polymerizable monomers (e.g., vinyl-based monomer) to implement a controlled polymerization reaction, has been strongly desired.
  • a radical polymerization initiator since a radical polymerization initiator has reactivity with a carbon-carbon double bond, a radical polymerization initiator normally does not exhibit sufficient polymerization activity when a carbon-carbon double bond is introduced into the molecule of the radical polymerization initiator. Specifically, a radical polymerization initiator that includes a carbon-carbon double bond and has the desired properties has not yet been obtained.
  • An organotellurium compound is known as a radical polymerization initiator that makes it possible to subject a vinyl-based monomer or the like to radical polymerization while controlling the molecular weight distribution and the like (see Patent Literature 2 and 3).
  • An object of the invention is to provide a radical polymerization initiator that is useful for producing a polymer that includes a double bond at the molecular terminal, and can be applied to a wide variety of radically polymerizable monomers to implement a controlled polymerization reaction, and a method for producing a polymer that utilizes the radical polymerization initiator.
  • the inventors conducted extensive studies with regard to a radical polymerization initiator that is used for a living radical polymerization reaction in order to solve the above problem. As a result, the inventors found that a wide variety of radically polymerizable monomers can be polymerized in a controlled manner, and a polymer that includes a double bond at the molecular terminal can be efficiently obtained by subjecting a radically polymerizable monomer to a living radical polymerization reaction in the presence of a radical polymerization initiator that includes an organotellurium compound that includes at least one non-aromatic carbon-carbon double bond at the 3-position. This finding has led to the completion of the invention.
  • R 1 represents a group selected from an alkyl group, a substituted or unsubstituted cycloalkyl group, a substituted or unsubstituted aryl group, and a substituted or unsubstituted heteroaromatic ring group
  • each of R 2 and R 3 independently represents an atom or a group selected from a hydrogen atom, an aliphatic hydrocarbon group, a substituted or unsubstituted aryl group, a substituted or unsubstituted heteroaromatic ring group, a halogen atom, a carboxyl group, a hydrocarbyloxycarbonyl group, a cyano group, and an amide group
  • each of R 4 , R 5 , and R 6 independently represents an atom or a group selected from a hydrogen atom, an aliphatic hydrocarbon group, a substituted or unsubstituted aryl group, a substituted or unsubstituted heteroaromatic ring group,
  • R 7 represents a group selected from an alkyl group, a substituted or unsubstituted cycloalkyl group, a substituted or unsubstituted aryl group, and a substituted or unsubstituted heteroaromatic ring group
  • each of R 8 and R 9 independently represents an atom or a group selected from a hydrogen atom, an aliphatic hydrocarbon group, a substituted or unsubstituted aryl group, a substituted or unsubstituted heteroaromatic ring group, a halogen atom, a carboxyl group, a hydrocarbyloxycarbonyl group, a cyano group, and an amide group
  • the wavy line represents that the group represented by the formula (2) is bonded to the carbon atom included in the formula (1) that forms the double bond.
  • a method for producing a polymer including subjecting a radically polymerizable monomer to radical polymerization in a state in which the radical polymerization initiator according to (1) is present in a polymerization system.
  • R 10 and R 11 independently represents a group selected from an alkyl group, a substituted or unsubstituted cycloalkyl group, a substituted or unsubstituted aryl group, and a substituted or unsubstituted heteroaromatic ring group.
  • the aspects of the invention thus provide a radical polymerization initiator that is useful for producing a polymer that includes a double bond at the molecular terminal, and can be applied to a wide variety of radically polymerizable monomers to implement a controlled polymerization reaction, and a method for producing a polymer that utilizes the radical polymerization initiator.
  • the expression “includes a double bond at the molecular terminal” used herein means that a group represented by (R 5 )(R 6 )C ⁇ (R 4 )—C(R 2 )(R 3 )— that is derived from the organotellurium compound represented by the formula (1) forms one of the terminals of the polymer chain.
  • a radical polymerization initiator and a method for producing a polymer according to the exemplary embodiments of the invention are described in detail below.
  • a radical polymerization initiator according to one embodiment of the invention includes the organotellurium compound represented by the formula (1).
  • R 1 in the formula (1) represents a group selected from an alkyl group, a substituted or unsubstituted cycloalkyl group, a substituted or unsubstituted aryl group, and a substituted or unsubstituted heteroaromatic ring group.
  • R 1 an alkyl group and a substituted or unsubstituted aryl group are preferable as R 1 .
  • substituted or unsubstituted used herein in connection with a group or the like means that the group or the like is unsubstituted, or substituted with a substituent.
  • the number of carbon atoms of the alkyl group that may be represented by R 1 is not particularly limited, but is preferably 1 to 10, more preferably 1 to 8, and still more preferably 1 to 5, from the viewpoint of availability.
  • Examples of the alkyl group that may be represented by R 1 include a linear alkyl group such as a methyl group, an ethyl group, an n-propyl group, an n-butyl group, an n-pentyl group, an n-hexyl group, an n-heptyl group, an n-octyl group, an n-nonyl group, and an n-decyl group; and a branched alkyl group such as an isopropyl group, a sec-butyl group, and a tert-butyl group.
  • a linear alkyl group such as a methyl group, an ethyl group, an n-propyl group, an n-butyl group, an n-pentyl group, an n-hexyl group, an n-heptyl group, an n-octyl group, an n-nonyl group, and
  • the number of carbon atoms of the cycloalkyl group (that is substituted or unsubstituted) that may be represented by R 1 is normally 3 to 10.
  • the number of carbon atoms of the cycloalkyl group is preferably 3 to 8, and more preferably 5 or 6, from the viewpoint of availability.
  • Examples of the cycloalkyl group (that is substituted or unsubstituted) that may be represented by R 1 include a cyclopropyl group, a cyclobutyl group, a cyclopentyl group, a cyclohexyl group, a cycloheptyl group, a cyclooctyl group, and the like.
  • a substituent that may substitute the cycloalkyl group (that is substituted or unsubstituted) that may be represented by R 1 is not particularly limited as long as the substituent does not hinder the polymerization reaction.
  • the substituent include a halogen atom such as a fluorine atom, a chlorine atom, a bromine atom, and an iodine atom; a hydroxyl group; an alkyl group having 1 to 8 carbon atoms, such as a methyl group, an ethyl group, an n-propyl group, and an isopropyl group; an alkoxy group having 1 to 8 carbon atoms, such as a methoxy group and an ethoxy group: an amino group; a nitro group; a cyano group; a group represented by —CORa (wherein Ra represents an alkyl group having 1 to 8 carbon atoms, such as a methyl group, an ethyl group, an n-propyl group
  • the number of carbon atoms of the aryl group (that is substituted or unsubstituted) that may be represented by R 1 is normally 6 to 20.
  • the number of carbon atoms of the aryl group is preferably 6 to 15, and more preferably 6 to 10, from the viewpoint of availability.
  • aryl group that is substituted or unsubstituted
  • examples of the aryl group include a phenyl group, a 1-naphthyl group, a 2-naphthyl group, an anthranyl group, and the like.
  • a substituent that may substitute the aryl group (that is substituted or unsubstituted) is not particularly limited as long as the substituent does not hinder the polymerization reaction.
  • Examples of the substituent include those mentioned above in connection with the cycloalkyl group (that is substituted or unsubstituted).
  • the number of carbon atoms of the heteroaromatic ring group (that is substituted or unsubstituted) that may be represented by R 1 is normally 1 to 15.
  • the number of carbon atoms of the heteroaromatic ring group is preferably 3 to 15, and more preferably 4 to 10, from the viewpoint of availability.
  • heteroaromatic ring group examples include a 5-membered heteroaromatic ring group such as a pyrrolyl group, an imidazolyl group, a furyl group, a thienyl group, an oxazolyl group, and a thiazolyl group; a 6-membered heteroaromatic ring group such as a pyridyl group, a pyrimidyl group, a pyridazyl group, and a pyrazinyl group; a fused heteroaromatic ring group such as a benzimidazolyl group, a quinolyl group, and a benzofuranyl group; and the like.
  • a 5-membered heteroaromatic ring group such as a pyrrolyl group, an imidazolyl group, a furyl group, a thienyl group, an oxazolyl group, and a thiazolyl group
  • a substituent that may substitute the heteroaromatic ring group (that is substituted or unsubstituted) is not particularly limited as long as the substituent does not hinder the polymerization reaction.
  • Examples of the substituent include those mentioned above in connection with the cycloalkyl group (that is substituted or unsubstituted).
  • Each of R 2 and R 3 in the formula (1) independently represents an atom or a group selected from a hydrogen atom, an aliphatic hydrocarbon group, a substituted or unsubstituted aryl group, a substituted or unsubstituted heteroaromatic ring group, a halogen atom, a carboxyl group, a hydrocarbyloxycarbonyl group, a cyano group, and an amide group.
  • a hydrogen atom and an aliphatic hydrocarbon group are preferable as R 2 and R 3 .
  • the number of carbon atoms of the aliphatic hydrocarbon group that may be represented by R 1 and R 3 is preferably 1 to 10, more preferably 1 to 8, and still more preferably 1 to 5.
  • Examples of the aliphatic hydrocarbon group that may be represented by R 2 and R 3 include an alkyl group having 1 to 10 carbon atoms, such as a methyl group and an ethyl group; an alkenyl group having 2 to 10 carbon atoms, such as a 1-propenyl group and a 2-propenyl group; an alkynyl group having 2 to 10 carbon atoms, such as a 1-propynyl group and a 2-propynyl group; a cycloalkyl group having 3 to 10 carbon atoms, such as a cyclopropyl group, a cyclobutyl group, a cyclopentyl group, and a cyclohexyl group; and the like.
  • substituted or unsubstituted aryl group that may be represented by R 2 and R 3 include those mentioned above in connection with the substituted or unsubstituted aryl group that may be represented by R.
  • substituted or unsubstituted heteroaromatic ring group that may be represented by R 2 and R 3 include those mentioned above in connection with the substituted or unsubstituted heteroaromatic ring group that may be represented by R 1 .
  • halogen atom examples include a fluorine atom, a chlorine atom, a bromine atom, an iodine atom, and the like.
  • the number of carbon atoms of the hydrocarbyloxycarbonyl group that may be represented by R 2 and R 3 is preferably 2 to 10, more preferably 2 to 8, and still more preferably 2 to 5.
  • hydrocarbyloxycarbonyl group examples include an alkyloxycarbonyl group such as a methyloxycarbonyl group and an ethyloxycarbonyl group; an alkenyloxycarbonyl group such as
  • an ethenyloxycarbonyl group and a 2-propenyloxycarbonyl group an alkynyloxycarbonyl group such as a propagyloxycarbonyl group; a substituted or unsubstituted aryloxycarbonyl group such as a phenoxycarbonyl group, a 4-methylphenyloxycarbonyl group, a 4-chlorophenoxycarbonyl group, a 1-naphthyloxycarbonyl group, and a 2-naphthyloxycarbonyl group; and the like.
  • Examples of the amide group that may be represented by R 2 and R 3 include a group represented by —C(X)—N(r 1 )(r 2 ) (wherein X represents an oxygen atom, a sulfur atom, or a selenium atom, and each of r 1 and r 2 independently represents a hydrogen atom or an organic group having 1 to 10 carbon atoms), a group represented by —SO 2 —N(r 1 )(r 2 ) (wherein r 1 and r 2 are the same as defined above), and a group represented by —N(r 1 )—C(O)-(r 2 ) (wherein r 1 and r 2 are the same as defined above).
  • Examples of the organic group that may be represented by r 1 and r 2 include a linear or branched alkyl group having 1 to 10 carbon atoms, such as a methyl group and an ethyl group; a linear or branched alkenyl group having 2 to 10 carbon atoms, such as a 1-propenyl group and a 2-propenyl group; a linear or branched alkynyl group having 2 to 10 carbon atoms, such as a 1-propynyl group and a 2-propynyl group; a cycloalkyl group having 3 to 10 carbon atoms, such as a cyclopropyl group, a cyclobutyl group, a cyclopentyl group, and a cyclohexyl group; an aryl group having 6 to 10 carbon atoms, such as a phenyl group and a 1-naphthyl group; an alkylcarbonyl group having 2 to 10 carbon atoms,
  • Examples of the group represented by —C(X)—N(r 1 )(r 2 ) include an aminocarbonyl group, a methylaminocarbonyl group, an ethylaminocarbonyl group, a benzylaminocarbonyl group, a phenylaminocarbonyl group, a dimethylaminocarbonyl group, a phenylmethylaminocarbonyl group, a dimethylaminothiocarbonyl group, a dimethylaminoselenocarbonyl group, and the like.
  • Examples of the group represented by —SO 2 —N(r 1 )(r 2 ) include an aminosulfonyl group, a methylaminosulfonyl group, a benzylaminosulfonyl group, a dimethylaminosulfonyl group, and the like.
  • Examples of the group represented by —N(r 1 )—C(O)-(r 2 ) include an acetylamino group, a benzoylamino group, and the like.
  • Each of R 4 , R 5 , and R 6 in the formula (1) independently represents an atom or a group selected from a hydrogen atom, an aliphatic hydrocarbon group, a substituted or unsubstituted aryl group, a substituted or unsubstituted heteroaromatic ring group, a halogen atom, a carboxyl group, a hydrocarbyloxycarbonyl group, a cyano group, an amide group, and a group represented by the formula (2).
  • a hydrogen atom, an aliphatic hydrocarbon group (including a ring that is formed by R 4 and R 5 that are bonded to each other), a hydrocarbyloxycarbonyl group, and the group represented by the formula (2) are preferable as R 4 , R 5 , and R 6 .
  • aliphatic hydrocarbon group that may be represented by R 4 , R 5 , and R 6 include those mentioned above in connection with the aliphatic hydrocarbon group that may be represented by R 2 and R 3 .
  • substituted or unsubstituted aryl group that may be represented by R 4 , R 5 , and R 6 include those mentioned above in connection with the substituted or unsubstituted aryl group that may be represented by R 1 .
  • substituted or unsubstituted heteroaromatic ring group that may be represented by R 4 , R 5 and R 6 include those mentioned above in connection with the substituted or unsubstituted heteroaromatic ring group that may be represented by R.
  • halogen atom that may be represented by R 4 , R 5 , and R 6 include those mentioned above in connection with the halogen atom that may be represented by R 2 and R.
  • hydrocarbyloxycarbonyl group that may be represented by R 4 , R 5 , and R 6 include those mentioned above in connection with the hydrocarbyloxycarbonyl group that may be represented by R 2 and R 3 .
  • amide group that may be represented by R 4 , R 5 , and R 6 include those mentioned above in connection with the amide group that may be represented by R 2 and R 3 .
  • R 7 in the formula (2) represents a group selected from an alkyl group, a substituted or unsubstituted cycloalkyl group, a substituted or unsubstituted aryl group, and a substituted or unsubstituted heteroaromatic ring group.
  • an alkyl group and a substituted or unsubstituted aryl group are preferable as R 7 .
  • alkyl group, the substituted or unsubstituted cycloalkyl group, the substituted or unsubstituted aryl group, and the substituted or unsubstituted heteroaromatic ring group that may be represented by R 7 include those mentioned above in connection with the alkyl group, the substituted or unsubstituted cycloalkyl group, the substituted or unsubstituted aryl group, and the substituted or unsubstituted heteroaromatic ring group that may be represented by R 1 .
  • Each of R 8 and R 9 in the formula (2) independently represents an atom or a group selected from a hydrogen atom, an aliphatic hydrocarbon group, a substituted or unsubstituted aryl group, a substituted or unsubstituted heteroaromatic ring group, a halogen atom, a carboxyl group, a hydrocarbyloxycarbonyl group, a cyano group, and an amide group.
  • a hydrogen atom and an aliphatic hydrocarbon group are preferable as R 8 and R 9 .
  • aliphatic hydrocarbon group, the substituted or unsubstituted aryl group, the substituted or unsubstituted heteroaromatic ring group, the halogen atom, the hydrocarbyloxycarbonyl group, and the amide group that may be represented by R 8 and R 9 include those mentioned above in connection with the aliphatic hydrocarbon group, the substituted or unsubstituted aryl group, the substituted or unsubstituted heteroaromatic ring group, the halogen atom, the hydrocarbyloxycarbonyl group, and the amide group that may be represented by R 2 and R 3 .
  • R 2 to R 6 are optionally bonded to each other to form a ring other than an aromatic ring.
  • a hydrocarbon ring is preferable as the ring other than an aromatic ring.
  • the ring is preferably a 5 to 7-membered ring, and more preferably a 6-membered ring.
  • Examples of the ring when the ring includes a double bond include a substituted or unsubstituted cyclopentene ring, a substituted or unsubstituted cyclohexene ring, a substituted or unsubstituted cycloheptene ring, and the like.
  • Examples of the ring when the ring does not include a double bond include a substituted or unsubstituted cyclopentane ring, a substituted or unsubstituted cyclohexane ring, a substituted or unsubstituted cycloheptane ring, and the like.
  • Examples of a substituent that may substitute the ring include those mentioned above in connection with the substituent that may substitute R 2 to R 1 .
  • organotellurium compound represented by the formula (1) include 3-methyltellanyl-1-propene, 3-methyltellanyl-2-methyl-1-propene, 3-methyltellanyl-2-phenyl-1-propene, 3-methyltellanyl-3-methyl-1-propene, 3-methyltellanyl-3-phenyl-1-propene, 3-methyltellanyl-3-cyclohexyl-1-propene, 3-methyltellanyl-3-cyano-1-propene, 3-ethyltellanyl-1-propene, 3-methyltellanyl-3-dimethylamninocarbonyl-1-propene, 3-[(n-propyl)tellanyl]-1-propene, 3-isopropyltellanyl-1-propene, 3-(n-butyl)tellanylpropene, 3-[(n-hexyl)tellanyl]-1-propene, 3-phenyltellanyl-1-propene, 3-[(p-methylphenyl)tellanyl]-1-propen
  • the organotellurium compound represented by the formula (1) may be obtained by reacting a compound represented by the following formula (4), a compound represented by the following formula (5), and metallic tellurium according to the method disclosed in WO2004/014962, for example.
  • X represents a halogen atom.
  • the halogen atom represented by X may be a fluorine atom, a chlorine atom, a bromine atom, or an iodine atom. Among these, a chlorine atom and a bromine atom are preferable.
  • R 1 in the formula (5) is the same as defined above.
  • M represents an alkali metal such as lithium, sodium, or potassium, an alkaline-earth metal such as magnesium or calcium, or copper.
  • m is 1 when M represents an alkali metal, is 2 when M represents an alkaline-earth metal, and is 1 or 2 when M represents copper.
  • M in the formula (5) represents magnesium
  • one of the two groups represented by R 1 may be a halogen atom.
  • the compound represented by the formula (5) may be a Grignard reagent.
  • metallic tellurium is suspended in a solvent in an inert gas atmosphere to prepare a suspension, and the compound represented by the formula (5) is added to the suspension to effect a reaction.
  • the compound represented by the formula (4) is added to the resulting reaction mixture to effect a reaction to obtain the organotellurium compound represented by the formula (1).
  • the compound represented by the formula (5) is normally used in an amount of 0.5 to 1.5 mol, and preferably 0.8 to 1.2 mol, based on 1 mol of metallic tellurium.
  • the compound represented by the formula (4) is normally used in an amount of 0.5 to 1.5 mol, and preferably 0.8 to 1.2 mol, based on 1 mol of metallic tellurium.
  • inert gas examples include nitrogen gas, helium gas, argon gas, and the like.
  • the solvent examples include an ether-based solvent such as diethyl ether and tetrahydrofuran; an amide-based solvent such as dimethylformamide; an aromatic solvent such as toluene; an aliphatic hydrocarbon-based solvent such as hexane; and the like.
  • Each of the compound represented by the formula (5) and the compound represented by the formula (4) is preferably added dropwise to the reaction system at a low temperature ( ⁇ 20 to 5° C.).
  • the reaction conditions are not particularly limited.
  • the reaction time is set to 5 minutes to 24 hours, and the reaction temperature is set to ⁇ 20 to 80° C.
  • Organotellurium compounds respectively represented by the following formulas (1a) to (1c) may be obtained as follows.
  • R 1 to R 9 are the same as defined above.
  • organotellurium compounds respectively represented by the formulas (1a) to (1c) may be obtained by reacting compounds respectively represented by the following formulas (4a) to (4c) as described above instead of the compound represented by the formula (4).
  • R 2 to R 9 are the same as defined above, provided that R 4 , R 5 , and R 6 are not the group represented by the formula (2), and X 1 and X 2 represent a halogen atom (preferably a chlorine atom or a bromine atom).
  • the compounds respectively represented by the formulas (4a) to (4c) are normally used in an amount of 0.25 to 0.75 mol, and preferably 0.4 to 0.6 mol, based on 1 mol of metallic tellurium.
  • the compound represented by the formula (5) is normally used in an amount of 0.5 to 1.5 mol, and preferably 0.8 to 1.2 mol, based on 1 mol of metallic tellurium.
  • the target product may be isolated by a known post-treatment operation and separation-purification means.
  • the reaction mixture is sequentially washed with deaerated water, a deaerated ammonium chloride aqueous solution, and a deaerated saturated sodium chloride solution, and the organic layer is dried and concentrated to obtain a crude product.
  • the resulting reaction product is optionally purified using a known purification method (e.g., vacuum distillation method) to obtain the target organotellurium compound having high purity.
  • the organotellurium compound represented by the formula (1) that is used as the radical polymerization initiator according to one embodiment of the invention includes at least one non-aromatic carbon-carbon double bond at the n-position with respect to Te.
  • a method for producing a polymer according to one embodiment of the invention includes subjecting a radically polymerizable monomer to radical polymerization in a state in which the radical polymerization initiator according to one embodiment of the invention is present in a polymerization system (i.e., in the presence of the radical polymerization initiator according to one embodiment of the invention).
  • the radically polymerizable monomer used in connection with one embodiment of the invention is not particularly limited as long as it is radically polymerizable.
  • the radically polymerizable monomer include an acrylic-based monomer such as methyl (meth)acrylate, ethyl (meth)acrylate, propyl (meth)acrylate, butyl (meth)acrylate, octyl (meth)acrylate, lauryl (meth)acrylate, 2-hydroxyethyl (meth)acrylate, cyclohexyl (meth)acrylate, methylcyclohexyl (meth)acrylate, isobornyl (meth)acrylate, cyclododecyl (meth)acrylate, glycidyl (meth)acrylate, (meth)acrylic acid, (meth)acrylamide, N-methyl(meth)acrylamide.
  • N-isopropyl(meth)acrylamide N,N-dimethyl(meth)acrylamide, N-(2-dimethylaminoethyl)(meth)acrylamide, N-(3-dimethylaminopropyl)(meth)acrylamide, 2-(dimethylamino)ethyl (meth)acrylate, 3-dimethylaminopropyl (meth)acrylate, hydroxyethyl (meth)acrylate, (meth)acrylonitrile, 2-hydroxy-3-(meth)acryloyloxypropyltrimethylammonium chloride, and (meth)acryloylaminoethyldimethylbenzylammonium chloride (Note that the term “(meth)acrylic acid” used herein refers to acrylic acid or methacrylic acid (this definition also applies to (meth)acrylamide and the like));
  • styrene-based monomer such as styrene, ⁇ -methylstyrene, 2-methylstyrene, 3-methylstyrene, 4-methylstyrene, 4-methoxystyrene, 4-tert-butylstyrene, 4-n-butylstyrene, 4-tert-butoxystyrene, 2-hydroxymethylstyrene, 2-chlorostyrene, 4-chlorostyrene, 2,4-dichlorostyrene, 1-vinylnaphthalene, divinylbenzene, 4-styrenesulfonic acid, and an alkali metal salt (e.g., sodium salt and potassium salt) thereof; an ⁇ -olefin-based monomer such as ethylene, propene, 1-butene, l-pentene, 1-hexene, l-octene, and 1-decene; a vinyl-based monomer such as 2-vinylthio
  • radically polymerizable monomers may be used either alone or in combination.
  • the method for producing a polymer according to one embodiment of the invention can implement a controlled polymerization reaction using a wide variety of radically polymerizable monomers as compared with known atom transfer radical polymerization that utilizes an allyl halide as a polymerization initiator to introduce a carbon-carbon double bond into the polymerization-initiation terminal. Therefore, the method for producing a polymer according to one embodiment of the invention can particularly suitably be used when using a radically polymerizable monomer for which it is difficult to implement a controlled polymerization reaction using a known method.
  • the radically polymerizable monomer that is particularly suitably used when implementing the method for producing a polymer according to one embodiment of the invention includes at least one radically polymerizable monomer selected from (meth)acrylates that include a functional group selected from a hydroxyl group, an amino group, and an ammonium group, (meth)acrylic acids, (meth)acrylamides, ⁇ -olefins, a vinyl-based monomer that includes a vinyl group that is not conjugate to an aromatic ring, and a conjugated diene-based monomer.
  • the amount of the organotellurium compound represented by the formula (1) and the amount of the radically polymerizable monomer may be appropriately adjusted taking account of the molecular weight and the molecular weight distribution of the desired polymer.
  • the organotellurium compound represented by the formula (1) is normally used in an amount of 0.00005 to 0.2 mol, and preferably 0.0001 to 0.02 mol, based on 1 mol of the radically polymerizable monomer.
  • Radical polymerization may be effected by charging a container (in which the internal atmosphere has been replaced by an inert gas (e.g., nitrogen gas, helium gas, or argon gas) with the organotellurium compound represented by the formula (1), the radically polymerizable monomer, and an optional solvent, and stirring the mixture at a specific temperature for a specific time.
  • an inert gas e.g., nitrogen gas, helium gas, or argon gas
  • a solvent that is normally used for a radical polymerization reaction may be used as the solvent.
  • the solvent include aromatic hydrocarbons such as benzene and toluene; ketones such as acetone and methyl ethyl ketone; esters such as ethyl acetate; ethers such as dioxane and tetrahydrofuran (THF); amides such as N,N-dimethylformamide (DMF); sulfur-containing compounds such as dimethyl sulfoxide (DMSO); alcohols such as methanol, ethanol, isopropanol, and n-butanol; halogen-containing compounds such as chloroform, carbon tetrachloride, and trifluoromethylbenzene; cellosolve and a derivative thereof such as ethyl cellosolve, butyl cellosolve, and 1-methoxy-2-propanol; water; and the like.
  • the solvent is used in an amount of 0.01 to 50 mL, preferably 0.05 to 10 mL, and more preferably 0.1 to 5 mL, based on 1 g of the radically polymerizable monomer, for example.
  • the reaction temperature and the reaction time may be appropriately adjusted.
  • the reaction temperature is normally set to 20 to 150° C., and preferably 40 to 100° C.
  • the reaction time is normally set to 1 minute to 100 hours, and preferably 0.1 to 30 hours.
  • the reaction is normally effected under normal pressure. Note that the reaction may be effected under pressure, or may be effected under reduced pressure.
  • the radically polymerizable monomer may be subjected to radical polymerization in a state in which an azo-based radical generator is further present in the polymerization system.
  • the polymerization reaction is effected in the presence of the azo-based radical generator, the polymerization reaction is further promoted, and a polymer can be efficiently obtained.
  • An arbitrary azo-based radical generator that is normally used for radical polymerization as a polymerization initiator or a polymerization promoter may be used as the azo-based radical generator.
  • azo-based radical generator examples include
  • azo-based radical generators may be used either alone or in combination.
  • 2,2′-azobis(2,4-dimethylvaleronitrile) ADVN
  • 2,2′-azobis(4-methoxy-2,4-dimethylvaleronitrile) are preferable when effecting the polymerization reaction at a low temperature (40° C. or less).
  • 2,2′-Azobis(isobutylonitrile) AIBN
  • 2,2′-azobis(2-methylbutyronitrile) AMBN
  • 1,1′-azobis(1-acetoxy-1-phenylethane) are preferable when effecting the polymerization reaction at a medium temperature (40 to 80° C.).
  • 1,1′-Azobis(cyclohexane-1-carbonitrile) ACBN
  • 2-cyano-2-propylazoformamide 2-cyano-2-propylazoformamide
  • 2,2′-azobis(N-butyl-2-methylpropionamide) 2,2′-azobis(N-cyclohexyl-2-methylpropionamide)
  • 2,2′-azobis(2,4,4-trimethylpentane) are preferable when effecting the polymerization reaction at a high temperature (80° C. or more).
  • the azo-based radical generator When using the azo-based radical generator, the azo-based radical generator is used in an amount of 0.01 to 100 mol, preferably 0.05 to 10 mol, and more preferably 0.05 to 2 mol, based on 1 mol of the organotellurium compound represented by the formula (1).
  • the polymerization reaction may be effected in a state in which light is applied to the polymerization system (i.e., while applying light to the polymerization system).
  • the polymerization reaction When the polymerization reaction is effected in a state in which light is applied to the polymerization system, the polymerization reaction is further promoted, and a polymer can be efficiently obtained.
  • Ultraviolet rays (light having a wavelength of 200 to 380 nm) or visible light (light having a wavelength of 380 to 830 nm) is preferable as light applied to the polymerization system.
  • Light may be applied to the polymerization system using a method that is normally used when effecting a photopolymerization reaction.
  • a light source such as a low-pressure mercury lamp, a medium-pressure mercury lamp, a high-pressure mercury lamp, an ultra-high-pressure mercury lamp, a chemical lamp, a black light lamp, a microwave-excited mercury lamp, a metal halide lamp, a xenon lamp, a krypton lamp, or an LED lamp.
  • the azo-based radical generator and the application of light may be used in combination. However, the polymerization reaction is normally promoted sufficiently when either the azo-based radical generator or the application of light is used.
  • the radically polymerizable monomer may be subjected to radical polymerization in a state in which the ditelluride compound represented by the formula (3) is further present in the polymerization system.
  • the polymerization reaction is effected in the presence of the ditelluride compound represented by the formula (3), it is possible to more advantageously control the polymerization reaction, and obtain a polymer having a molecular weight close to the theoretical value and a narrow molecular weight distribution.
  • Each of R 10 and R 11 in the formula (3) independently represents a group selected from an alkyl group, a substituted or unsubstituted cycloalkyl group, a substituted or unsubstituted aryl group, and a substituted or unsubstituted heteroaromatic ring group.
  • alkyl group, the substituted or unsubstituted cycloalkyl group, the substituted or unsubstituted aryl group, and the substituted or unsubstituted heteroaromatic ring group that may be represented by R 10 and R 11 include those mentioned above in connection with the alkyl group, the substituted or unsubstituted cycloalkyl group, the substituted or unsubstituted aryl group, and the substituted or unsubstituted heteroaromatic ring group that may be represented by R 1 .
  • ditelluride compound represented by the formula (3) include dimethyl ditelluride, diethyl ditelluride, di(n-propyl) ditelluride, diisopropyl ditelluride, dicyclopropyl ditelluride, di(n-butyl) ditelluride, di(sec-butyl) ditelluride, di(tert-butyl) ditelluride, dicyclobutyl ditelluride, diphenyl ditelluride, bis(p-methoxyphenyl) ditelluride, bis(p-aminophenyl) ditelluride, bis(p-nitrophenyl) ditelluride, bis(p-cyanophenyl) ditelluride, bis(p-sulfonylphenyl) ditelluride, bis(2-naphthyl) ditelluride, 4,4′-dypyridyl ditelluride, and the like.
  • These ditelluride compounds may be used either alone or in combination.
  • the ditelluride compound represented by the formula (3) is used in an amount of 0.01 to 100 mol, preferably 0.1 to 10 mol, and more preferably 0.1 to 5 mol, based on 1 mol of the organotellurium compound represented by the formula (1), for example.
  • ditelluride compound represented by the formula (3) may be used in combination with the azo-based radical generator, or may be used in combination with the application of light.
  • the polymer may be isolated and purified using an ordinary method.
  • the solvent and the residual radically polymerizable monomer may be evaporated from the reaction solution under reduced pressure to isolate the polymer, or the reaction solution may be poured into a poor solvent to precipitate the polymer.
  • the molecular weight of a polymer that is obtained by the method for producing a polymer according to one embodiment of the invention can be adjusted by adjusting the reaction time and the amount of organotellurium compound.
  • the number average molecular weight of the polymer is 500 to 1,000,000, and preferably 1,000 to 50,000.
  • the molecular weight distribution (Mw/Mn) of the polymer is normally 1.01 to 2.50, preferably 1.01 to 2.00, more preferably 1.01 to 1.50, still more preferably 1.01 to 1.30, and most preferably 1.01 to 1.15.
  • the method for producing a polymer according to one embodiment of the invention can produce a copolymer when two or more radically polymerizable monomers are used.
  • the method for producing a polymer according to one embodiment of the invention can produce a random copolymer when two or more radically polymerizable monomers are simultaneously present in the polymerization system.
  • the method for producing a polymer according to one embodiment of the invention can produce a block copolymer when two or more radically polymerizable monomers are sequentially reacted, since the polymerization reaction proceeds in a living manner (described later).
  • the growing terminal of the polymer chain during the polymerization reaction effected by the method for producing a polymer according to one embodiment of the invention is a highly reactive organotellurium site (R 1 —Te— or R 7 —Te—) derived from the radical polymerization initiator according to one embodiment of the invention, and has living properties.
  • the growing terminal of the polymer chain that has living properties When the growing terminal of the polymer chain that has living properties is exposed to air, the growing terminal is substituted with a hydrogen atom or a hydroxyl group, and is inactivated.
  • the other terminal (polymerization-initiation terminal) of the polymer obtained by the method for producing a polymer according to one embodiment of the invention is a group represented by (R 5 )(R 6 )C ⁇ C(R 4 )—C(R 2 )(R 3 )— that is derived from the organotellurium compound represented by the formula (1).
  • the method for producing a polymer according to one embodiment of the invention can efficiently produce a polymer that includes a double bond at the molecular terminal, has a controlled molecular weight and molecular weight distribution, and is useful as a macromonomer and the like.
  • the 1 H-NMR measurement was performed using an NMR spectrometer “BRUKER-500” (manufactured by BRUKER) (solvent: CDCl 3 or d-DMSO).
  • the gas chromatography measurement was performed using a gas chromatograph “GC2010” (manufactured by Shimadzu Corporation) and a column “ZB-5” (manufactured by Phenomenex). The quantitative determination was performed based on an internal standard method using mesitylene.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the polymer were determined as polystyrene-equivalent values by gel permeation chromatography (GPC) measurement using a GPC system “HLC-8220” (manufactured by Tosoh Corporation) (column: TSK-GEL G6000HHR, G5000HHR, G4000HHR, and G2500HHR (manufactured by Tosoh Corporation) (that were sequentially connected), eluent: tetrahydrofuran (THF)).
  • GPC gel permeation chromatography
  • a 300 mL three-necked flask was charged with 5.23 g (41 mmol) of metallic tellurium (manufactured by Aldrich (hereinafter the same)) and 45 mL of THF in a nitrogen atmosphere to prepare a suspension.
  • the suspension was cooled to 0° C. with stirring.
  • 45.0 mL (43.0 mmol) of methyllithium (1.10 M diethyl ether solution, manufactured by Kanto Chemical Co., Inc. (hereinafter the same)) was added dropwise to the suspension over 10 minutes while cooling the suspension with stirring. After the dropwise addition, the mixture contained in the three-necked flask was stirred at room temperature (25° C.) for 20 minutes to obtain a reaction solution in which the metallic tellurium had completely disappeared.
  • a 300 mL three-necked flask was charged with 8.75 g (68.6 mmol) of metallic tellurium and 90 mL of THF in a nitrogen atmosphere to prepare a suspension.
  • the suspension was cooled to 0° C. with stirring.
  • a 300 mL three-necked flask was charged with 11.48 g (90 mmol) of metallic tellurium and 86 mL of THF in a nitrogen atmosphere to prepare a suspension.
  • the suspension was cooled to 0° C. with stirring.
  • 86.0 mL (94.5 mmol) of methyllithium (1.10 M diethyl ether solution) was added dropwise to the suspension over 10 minutes while cooling the suspension with stirring. After the dropwise addition, the mixture contained in the three-necked flask was stirred at room temperature (25° C.) for 20 minutes to obtain a reaction solution in which the metallic tellurium had completely disappeared.
  • the reaction solution was cooled to 0° C. with stirring. 11.4 g (94.5 mmol) of allyl bromide (manufactured by Tokyo Chemical Industry Co., Ltd. (hereinafter the same)) was added to the reaction solution while cooling the reaction solution with stirring. After reacting the mixture contained in the three-necked flask for 2 hours with stirring, the reaction solution was returned to room temperature.
  • allyl bromide manufactured by Tokyo Chemical Industry Co., Ltd. (hereinafter the same)
  • the resulting reaction solution was sequentially washed with deaerated water, a deaerated saturated NH 4 Cl aqueous solution, and a deaerated saturated NaCl aqueous solution.
  • the organic layer i.e., the reaction solution subjected to washing
  • the filtrate was concentrated under reduced pressure, and the concentrate was subjected to vacuum distillation (33 mmHg, 55° C.) to obtain 6.55 g (yield: 40%) of 3-methyltellanyl-1-propene as a yellow oily product.
  • a 300 mL three-necked flask was charged with 6.38 g (50 mmol) of metallic tellurium and 50 mL of THF in a nitrogen atmosphere to prepare a suspension.
  • the suspension was cooled to 0° C. with stirring.
  • 48.6 mL (52.5 mmol) of phenyllithium (1.08 M cyclohexane-diethyl ether solution, manufactured by Kanto Chemical Co., Inc.) was added dropwise to the suspension over 10 minutes while cooling the suspension with stirring. After the dropwise addition, the mixture contained in the three-necked flask was stirred at room temperature (25° C.) for 20 minutes to obtain a reaction solution in which the metallic tellurium had completely disappeared.
  • reaction solution was cooled to 0° C. with stirring. 6.35 g (52.5 mmol) of allyl bromide was added to the reaction solution while cooling the reaction solution with stirring. After reacting the mixture contained in the three-necked flask for 2 hours with stirring, the reaction solution was returned to room temperature.
  • the resulting reaction solution was sequentially washed with deaerated water, a deaerated saturated NH 4 Cl aqueous solution, and a deaerated saturated NaCl aqueous solution.
  • the organic layer i.e., the reaction solution subjected to washing
  • the filtrate was concentrated under reduced pressure, and the concentrate was subjected to vacuum distillation (2.0 mmnHg, 70° C.) to obtain 5.6 g (yield: 46%) of 3-phenyltellanyl-1-propene as a yellow oily product.
  • a 300 mL three-necked flask was charged with 3.76 g (29.5 mmol) of metallic tellurium and 38 mL of THF in a nitrogen atmosphere to prepare a suspension.
  • the suspension was cooled to 0° C. with stirring.
  • 19.4 mL (31.0 mmol) of n-butyllithium (1.6 M hexane solution) was added dropwise to the suspension over 10 minutes while cooling the suspension with stirring.
  • the mixture contained in the three-necked flask was stirred at room temperature (25° C.) for 20 minutes to obtain a reaction solution in which the metallic tellurium had completely disappeared.
  • reaction solution was cooled to 0° C. with stirring.
  • 5.0 g (31.0 mmol) of 3-bromocyclohexene manufactured by Tokyo Chemical Industry Co., Ltd. was added to the reaction solution while cooling the reaction solution with stirring. After reacting the mixture contained in the three-necked flask for 2 hours with stirring, the reaction solution was returned to room temperature.
  • the resulting reaction solution was sequentially washed with deaerated water, a deaerated saturated NH 4 Cl aqueous solution, and a deaerated saturated NaCl aqueous solution.
  • the organic layer i.e., the reaction solution subjected to washing
  • the filtrate was concentrated under reduced pressure, and the concentrate was subjected to vacuum distillation (1.0 mmHg, 82° C.) to obtain 4.47 g (yield: 57%) of 3-[(n-butyl)tellanyl]-1-cyclohexene as a yellow oily product.
  • a 300 mL three-necked flask was charged with 3.39 g (26.6 mmol) of metallic tellurium and 25 mL of THF in a nitrogen atmosphere to prepare a suspension.
  • the suspension was cooled to 0° C. with stirring.
  • 25.1 mL (27.9 mmol) of methyllithium (1.11 M diethyl ether solution) was added dropwise to the suspension over 10 minutes while cooling the suspension with stirring.
  • the mixture contained in the three-necked flask was stirred at room temperature (25° C.) for 20 minutes to obtain a reaction solution in which the metallic tellurium had completely disappeared.
  • the reaction solution was cooled to 0° C. with stirring.
  • 5.0 g (27.9 mmol) of methyl 2-(bromomethyl)acrylate manufactured by Tokyo Chemical Industry Co., Ltd. was added to the reaction solution while cooling the reaction solution with stirring. After reacting the mixture contained in the three-necked flask for 2 hours with stirring, the reaction solution was returned to room temperature.
  • the resulting reaction solution was sequentially washed with deaerated water, a deaerated saturated NH 4 Cl aqueous solution, and a deaerated saturated NaCl aqueous solution.
  • the organic layer i.e., the reaction solution subjected to washing
  • the filtrate was concentrated under reduced pressure, and the concentrate was subjected to vacuum distillation (1.0 mmHg, 52° C.) to obtain 2.3 g (yield: 36%) of methyl 2-(methyltellanylmethyl)acrylate as a yellow oily product.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried to obtain an isoprene-acrylonitrile random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 93% and 84%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-acrylonitrile random copolymer determined by GPC were 7,060, 6,130, and 1.15, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that 1,1′-azobis(cyclohexane-1-carbonitrile) was not added, and light was applied to the polymerization system during the polymerization reaction using an LED lamp (output: 6 W, 5% ND filter was used), to obtain an isoprene-acrylonitrile random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 88% and 81%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-acrylonitrile random copolymer determined by GPC were 6,730, 6,100, and 1.09, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that dimethyl ditelluride was not added, to obtain an isoprene-acrylonitrile random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 92% and 82%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-acrylonitrile random copolymer determined by GPC were 8,690, 6,980, and 1.25, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that dimethyl ditelluride and 1,1′-azobis(cyclohexane-1-carbonitrile) were not added, and the polymerization reaction time was changed to 72 hours, to obtain an isoprene-acrylonitrile random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 75% and 63%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-acrylonitrile random copolymer determined by GPC were 4,160, 3,080, and 1.35, respectively.
  • a 30 mL glass reaction vessel was charged with 2.56 g (20 mmol) of n-butyl acrylate (manufactured by Wako Pure Chemical Industries, Ltd. (hereinafter the same)), 36.7 mg (0.20 mmol) of 3-methyltellanyl-1-propene obtained in Example 1, 16.4 mg (0.10 mmol) of azobisisobutyronitrile (manufactured by Wako Pure Chemical Industries, Ltd. (hereinafter the same)), and 0.24 g of mesitylene (internal standard), and the mixture was stirred at 60° C. for 1 hour to effect a polymerization reaction.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried to obtain an n-butyl acrylate polymer.
  • the conversion ratio of n-butyl acrylate determined by gas chromatography was 91%.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the n-butyl acrylate polymer determined by GPC were 18,970, 15,240, and 1.25, respectively.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried to obtain an n-butyl acrylate-methyl methacrylate block copolymer.
  • the conversion ratio of methyl methacrylate determined by gas chromatography was 100%.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the n-butyl acrylate-methyl methacrylate block copolymer determined by GPC were 50,900, 29,600, and 1.71, respectively.
  • n-butyl acrylate-methyl methacrylate block copolymer included a terminal double bond in a ratio of 88%.
  • a polymerization reaction was effected in the same manner as in Example 9, except that 2.08 g (20 mmol) of styrene (manufactured by Tokyo Chemical Industry Co., Ltd. (hereinafter the same)) was used instead of n-butyl acrylate, to obtain a styrene polymer.
  • the conversion ratio of styrene determined by gas chromatography was 91%.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the styrene polymer determined by GPC were 10,860, 8,150, and 1.33, respectively.
  • a 30 mL glass reaction vessel was charged with 2.08 g (20 mmol) of styrene, 36.7 mg (0.20 mmol) of 3-methyltellanyl-1-propene obtained in Example 1, 16.4 mg (0.10 mmol) of azobisisobutyronitrile, and 0.24 g of mesitylene (internal standard), and the mixture was stirred at 60° C. for 1 hour to effect a polymerization reaction. After the addition of 1.00 g (10 mmol) of methyl methacrylate and 28.5 mg (0.1 mmol) of dimethyl ditelluride obtained in Synthesis Example 1 to the reaction vessel, the mixture was stirred at 80° C. for 15 hours to effect a polymerization reaction.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried to obtain a styrene-methyl methacrylate block copolymer.
  • the conversion ratio of methyl methacrylate determined by gas chromatography was 100%.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the styrene-methyl methacrylate block copolymer determined by GPC were 26,600, 18,800, and 1.41, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that 1.00 g (10 mmol) of methyl methacrylate was used instead of acrylonitrile, to obtain an isoprene-methyl methacrylate random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of methyl methacrylate determined by gas chromatography were 97% and 90%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-methyl methacrylate random copolymer determined by GPC were 9,110, 7,530, and 1.21, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that 1.28 g (10 mmol) of n-butyl acrylate was used instead of acrylonitrile, to obtain an isoprene-n-butyl acrylate random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of n-butyl acrylate determined by gas chromatography were 99% and 87%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-n-butyl acrylate random copolymer determined by GPC were 5,800, 4,700, and 1.23, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that 1.04 g (10 mmol) of styrene was used instead of acrylonitrile, to obtain an isoprene-styrene random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of styrene determined by gas chromatography were 93% and 73%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-styrene random copolymer determined by GPC were 8,070, 6,580, and 1.19, respectively.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried to obtain a butadiene-acrylonitrile random copolymer.
  • the conversion ratio of 1,3-butadiene and the conversion ratio of acrylonitrile determined by gas chromatography were 81% and 58%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the butadiene-acrylonitrile random copolymer determined by GPC were 332,300, 223,000, and 1.49, respectively.
  • a 30 mL glass reaction vessel was charged with 0.68 g (10 mmol) of cis-1,3-pentadiene (manufactured by Tokyo Chemical Industry Co., Ltd.), 0.53 g (10 mmol) of acrylonitrile, 1.2 mg (0.0067 mmol) of 3-methyltellanyl-1-propene obtained in Example 1, 0.4 mg (0.0013 mmol) of dimethyl ditelluride, 0.8 mg (0.003 mmol) of 1,1′-azobis(cyclohexane-1-carbonitrile), and 0.24 g of mesitylene (internal standard), and the mixture was stirred at 80° C. for 38 hours to effect a polymerization reaction.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried to obtain a cis-1,3-pentadiene-acrylonitrile random copolymer.
  • the conversion ratio of cis-1,3-pentadiene and the conversion ratio of acrylonitrile determined by gas chromatography were 76% and 36% S, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the cis-1,3-pentadiene-acrylonitrile random copolymer determined by GPC were 89,400, 60,400, and 1.48, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that 49.1 mg (0.2 mmol) of 3-phenyltellanyl-1-propene obtained in Example 2 was used instead of 3-methyltellanyl-1-propene, and 8.2 mg (0.02 mmol) of diphenyl ditelluride (manufactured by Aldrich) was used instead of dimethyl ditelluride, to obtain an isoprene-acrylonitrile random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 91% and 82%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-acrylonitrile random copolymer determined by GPC were 5,740, 5,010, and 1.15, respectively.
  • a polymerization reaction was effected in the same manner as in Example 5, except that 52.9 mg (0.2 mmol) of 3-[(n-butyl)tellanyl]-1-cyclohexene obtained in Example 3 was used instead of 3-methyltellanyl-1-propene, and 7.5 mg (0.02 mmol) of dibutyl ditelluride obtained in Synthesis Example 2 was used instead of dimethyl ditelluride, to obtain an isoprene-acrylonitrile random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 91% and 84%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-acrylonitrile random copolymer determined by GPC were 7,770, 6,150, and 1.26, respectively.
  • a polymerization reaction was effected in the same manner as in Example 10, except that 48.3 mg (0.2 mmol) of methyl 2-(methyltellanylmethyl)acrylate obtained in Example 4 was used instead of 3-methyltellanyl-1-propene, to obtain an isoprene-acrylonitrile random copolymer.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 86% and 76%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the isoprene-acrylonitrile random copolymer determined by GPC were 8,190, 5,570, and 1.47, respectively.
  • a polymerization reaction was effected in the same manner as in Example 9, except that 3.14 g (20 mmol) of 2-(dimethylamino)ethyl methacrylate was used instead of n-butyl acrylate, to obtain a 2-(dimethylamino)ethyl methacrylate polymer.
  • the conversion ratio of 2-(dimethylamino)ethyl methacrylate determined by gas chromatography was 83%.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the 2-(dimethylamino)ethyl methacrylate polymer determined by GPC were 25,900, 19,300, and 1.34, respectively.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried.
  • the conversion ratio of isoprene and the conversion ratio of acrylonitrile determined by gas chromatography were 21% and 27%, respectively.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the resulting product determined by GPC were 370, 360, and 1.04, respectively. It was thus found that an oligomer was obtained by the polymerization reaction.
  • a 30 mL glass reaction vessel was charged with 28.7 mg (0.2 mmol) of copper(I) bromide, 34.7 mg (0.2 mmol) of N,N,N′,N′′,N′′-pentamethyldiethylenetriamine, 2 mL of toluene, 3.14 g (20 mmol) of 2-(dimethylamino)ethyl methacrylate, 24.2 mg (0.20 mmol) of allyl bromide, and 0.24 g of mesitylene (internal standard), and the mixture was stirred at 80° C. for 15 hours to effect a polymerization reaction.
  • the resulting polymerization reaction product was purified by evaporating a volatile component under reduced pressure, and the purified product was dried to obtain a 2-(dimethylamino)ethyl methacrylate polymer.
  • the conversion ratio of 2-(dimethylamino)ethyl methacrylate determined by gas chromatography was 42%.
  • the weight average molecular weight (Mw), the number average molecular weight (Mn), and the molecular weight distribution (Mw/Mn) of the 2-(dimethylamino)ethyl methacrylate polymer determined by GPC were 36,000, 13,300, and 2.71, respectively.
  • the 2-(dimethylamino)ethyl methacrylate polymer had a relatively wide molecular weight distribution.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Polymerization Catalysts (AREA)
US15/038,579 2013-11-27 2014-11-27 Radical polymerization initiator and method for producing polymers Abandoned US20160297755A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2013245352 2013-11-27
JP2013-245352 2013-11-27
PCT/JP2014/081334 WO2015080189A1 (fr) 2013-11-27 2014-11-27 Initiateur de polymérisation par voie radicalaire et procédé de production de polymères

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2014/081334 A-371-Of-International WO2015080189A1 (fr) 2013-11-27 2014-11-27 Initiateur de polymérisation par voie radicalaire et procédé de production de polymères

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US16/439,109 Division US10689336B2 (en) 2013-11-27 2019-06-12 Radical polymerization initiator and method for producing polymers

Publications (1)

Publication Number Publication Date
US20160297755A1 true US20160297755A1 (en) 2016-10-13

Family

ID=53199127

Family Applications (2)

Application Number Title Priority Date Filing Date
US15/038,579 Abandoned US20160297755A1 (en) 2013-11-27 2014-11-27 Radical polymerization initiator and method for producing polymers
US16/439,109 Active US10689336B2 (en) 2013-11-27 2019-06-12 Radical polymerization initiator and method for producing polymers

Family Applications After (1)

Application Number Title Priority Date Filing Date
US16/439,109 Active US10689336B2 (en) 2013-11-27 2019-06-12 Radical polymerization initiator and method for producing polymers

Country Status (5)

Country Link
US (2) US20160297755A1 (fr)
EP (1) EP3075748B1 (fr)
JP (1) JP6550610B2 (fr)
CN (1) CN105745230B (fr)
WO (1) WO2015080189A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10808065B2 (en) 2016-05-02 2020-10-20 Kyoto University Method for producing multibranched polymer and multibranched polymer

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017170250A1 (fr) * 2016-03-31 2017-10-05 日本ゼオン株式会社 Procédé de production de copolymère, et procédé de production de latex
CN110418806B (zh) * 2017-03-09 2022-02-22 Ａｇｃ株式会社 聚合物的制造方法
TWI733069B (zh) * 2017-12-31 2021-07-11 美商羅門哈斯電子材料有限公司 單體、聚合物及包含其的微影組合物
CN111848861B (zh) * 2019-04-30 2022-03-04 天津大学 一种基于有机碲与铂配位的响应型水凝胶及制备方法
CN114292354B (zh) * 2021-11-01 2023-06-16 深圳市森若新材科技有限公司 一种可应用于空调蓄冷的聚合物相变材料
CN116082545B (zh) * 2023-02-07 2024-04-05 苏州大学 一种近红外光诱导碲调控可逆-失活自由基聚合的方法

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5043477A (en) * 1987-07-13 1991-08-27 The United States Of America As Represented By The Secretary Of The Navy Methyl allyl telluride
US6274688B1 (en) * 1997-07-28 2001-08-14 Kaneka Corporation Functional groups-terminated vinyl polymers
US20100016191A1 (en) * 2008-07-18 2010-01-21 Harrison James J Copolymers Made With Allyl-Terminated Polyolefins And Unsaturated Acidic Reagents, Dispersants Using Same, and Methods of Making Same

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2335777C (fr) 1998-06-19 2008-08-19 Kaneka Corporation Procede de fabrication d'un polymere ramifie et polymere correspondant
JP4842887B2 (ja) 1998-06-19 2011-12-21 株式会社カネカ 枝分かれした重合体の製造方法及び重合体
JP4464821B2 (ja) * 2002-08-06 2010-05-19 大塚化学株式会社 有機テルル化合物、その製造方法、リビングラジカル重合開始剤、それを用いるポリマーの製造方法及びポリマー
WO2004014962A1 (fr) 2002-08-08 2004-02-19 Otsuka Chemical Co., Ltd. Procede de production de polymeres a radicaux libres et de polymeres
JP4107996B2 (ja) * 2003-04-25 2008-06-25 大塚化学株式会社 リビングラジカルポリマーの製造方法及びポリマー
JP2005344009A (ja) * 2004-06-03 2005-12-15 Shin Etsu Chem Co Ltd レジスト材料用高分子化合物及びその製造方法並びに化学増幅ポジ型レジスト材料
JP5193480B2 (ja) 2006-03-11 2013-05-08 大塚化学株式会社 リビングラジカルポリマーの製造方法およびポリマー
CN102344537B (zh) * 2010-07-30 2014-04-16 奇美实业股份有限公司 嵌段共聚物及以其制得的聚合物组成物
JP5963516B2 (ja) * 2011-04-28 2016-08-03 国立大学法人京都大学 ポリマーの製造方法及び該方法により製造されたポリマー

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5043477A (en) * 1987-07-13 1991-08-27 The United States Of America As Represented By The Secretary Of The Navy Methyl allyl telluride
US6274688B1 (en) * 1997-07-28 2001-08-14 Kaneka Corporation Functional groups-terminated vinyl polymers
US20100016191A1 (en) * 2008-07-18 2010-01-21 Harrison James J Copolymers Made With Allyl-Terminated Polyolefins And Unsaturated Acidic Reagents, Dispersants Using Same, and Methods of Making Same

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
"Vinyl Polymers", downloaded from http://pslc.ws/macrog/vinyl.htm (Year: 2018) *
Fónagy et al., Macromolecules 2007, 40, 1401-1407. *
Vojtova et al., Mat. Res. Soc. Symp. Proc. Vol. 774, 2003, O1.8.1-O1.8.15. *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10808065B2 (en) 2016-05-02 2020-10-20 Kyoto University Method for producing multibranched polymer and multibranched polymer

Also Published As

Publication number Publication date
WO2015080189A1 (fr) 2015-06-04
JPWO2015080189A1 (ja) 2017-03-16
JP6550610B2 (ja) 2019-07-31
EP3075748B1 (fr) 2020-11-18
EP3075748A4 (fr) 2017-06-14
US10689336B2 (en) 2020-06-23
CN105745230B (zh) 2019-08-13
EP3075748A1 (fr) 2016-10-05
US20190292146A1 (en) 2019-09-26
CN105745230A (zh) 2016-07-06

Similar Documents

Publication Publication Date Title
US10689336B2 (en) Radical polymerization initiator and method for producing polymers
US10414848B2 (en) Living radical polymerization initiator, method for producing polymer, and polymer
JP4107996B2 (ja) リビングラジカルポリマーの製造方法及びポリマー
TW200426159A (en) Manufacturing method for living radical polymer and the polymer therefrom
WO2006001496A1 (fr) Composé d’antimoine organique, procédé pour le produire, initiateur de polymérisation radicalaire vivant, procédé pour produire un polymère l’utilisant, et polymère
JP2017200882A (ja) 有機テルル化合物及びその製造方法並びにリビングラジカル重合開始剤及びそれを用いたビニル重合体の製造方法
TWI388580B (zh) 活性自由基聚合反應助觸媒
JP5176120B2 (ja) リビングラジカル重合開始剤及びそれを用いるポリマーの製造方法
WO2018159740A1 (fr) Procédé de production d'un polymère greffé, polymère greffé et initiateur pour polymère greffé
WO2017191766A1 (fr) Procédé de production d'un polymère multiramifié et polymère multiramifié
JP2007302737A (ja) リビングラジカルポリマーの製造方法
JP5963516B2 (ja) ポリマーの製造方法及び該方法により製造されたポリマー
JP7070897B2 (ja) 多分岐ポリマーの製造方法及び多分岐ポリマー、共役ジエンモノマー
US20190092890A1 (en) Method for producing copolymer, and method for producing latex
JP6619688B2 (ja) ビニル重合体の製造方法
JPWO2010052916A1 (ja) 官能基を有する重合体の製造方法及びそれにより得られるスターポリマー
JP4696275B2 (ja) インドール化合物の製法及び触媒
JP5374151B2 (ja) 重合開始剤
JP7550017B2 (ja) 有機ジテルリド化合物の精製方法
JPWO2020116144A1 (ja) 有機テルル化合物の製造方法およびビニル重合体の製造方法
JP2017197649A (ja) 重合体の製造方法

Legal Events

Date Code Title Description
AS Assignment

Owner name: ZEON CORPORATION, JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:BANDO, FUMIAKI;YAMAGO, SHIGERU;SIGNING DATES FROM 20160510 TO 20160511;REEL/FRAME:038687/0429

Owner name: KYOTO UNIVERSITY, JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:BANDO, FUMIAKI;YAMAGO, SHIGERU;SIGNING DATES FROM 20160510 TO 20160511;REEL/FRAME:038687/0429

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION