WO2018145517A1 - Method for catalyzing polymerization of vinyl monomers by means of transition metal nanoparticle - Google Patents

Method for catalyzing polymerization of vinyl monomers by means of transition metal nanoparticle Download PDF

Info

Publication number
WO2018145517A1
WO2018145517A1 PCT/CN2017/116807 CN2017116807W WO2018145517A1 WO 2018145517 A1 WO2018145517 A1 WO 2018145517A1 CN 2017116807 W CN2017116807 W CN 2017116807W WO 2018145517 A1 WO2018145517 A1 WO 2018145517A1
Authority
WO
WIPO (PCT)
Prior art keywords
acrylate
methacrylate
nanoparticles
monomer
vinyl
Prior art date
Application number
PCT/CN2017/116807
Other languages
French (fr)
Chinese (zh)
Inventor
唐华东
李小年
祝一峰
张攀攀
袁明
Original Assignee
浙江工业大学
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 浙江工业大学 filed Critical 浙江工业大学
Publication of WO2018145517A1 publication Critical patent/WO2018145517A1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers 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
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10Esters
    • C08F220/12Esters of monohydric alcohols or phenols
    • C08F220/16Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms
    • C08F220/18Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms with acrylic or methacrylic acids
    • C08F220/1804C4-(meth)acrylate, e.g. butyl (meth)acrylate, isobutyl (meth)acrylate or tert-butyl (meth)acrylate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F112/00Homopolymers 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
    • C08F112/02Monomers containing only one unsaturated aliphatic radical
    • C08F112/04Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F112/06Hydrocarbons
    • C08F112/08Styrene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F118/00Homopolymers 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 acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid
    • C08F118/02Esters of monocarboxylic acids
    • C08F118/04Vinyl esters
    • C08F118/08Vinyl acetate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F120/00Homopolymers 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
    • C08F120/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F120/04Acids; Metal salts or ammonium salts thereof
    • C08F120/06Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F120/00Homopolymers 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
    • C08F120/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F120/10Esters
    • C08F120/12Esters of monohydric alcohols or phenols
    • C08F120/14Methyl esters, e.g. methyl (meth)acrylate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F120/00Homopolymers 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
    • C08F120/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F120/10Esters
    • C08F120/12Esters of monohydric alcohols or phenols
    • C08F120/16Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms
    • C08F120/18Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms with acrylic or methacrylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F120/00Homopolymers 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
    • C08F120/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F120/10Esters
    • C08F120/22Esters containing halogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F120/00Homopolymers 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
    • C08F120/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F120/42Nitriles
    • C08F120/44Acrylonitrile
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F120/00Homopolymers 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
    • C08F120/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F120/52Amides or imides
    • C08F120/54Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
    • C08F120/56Acrylamide; Methacrylamide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F126/00Homopolymers 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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen
    • C08F126/06Homopolymers 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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen by a heterocyclic ring containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F126/00Homopolymers 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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen
    • C08F126/06Homopolymers 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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen by a heterocyclic ring containing nitrogen
    • C08F126/10N-Vinyl-pyrrolidone
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F136/00Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
    • C08F136/02Homopolymers 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
    • C08F136/04Homopolymers 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
    • C08F136/08Isoprene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00Copolymers 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
    • C08F220/02Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10Esters
    • C08F220/12Esters of monohydric alcohols or phenols
    • C08F220/14Methyl esters, e.g. methyl (meth)acrylate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F226/00Copolymers 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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen
    • C08F226/06Copolymers 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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen by a heterocyclic ring containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/50Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides selected from alkaline earth metals, zinc, cadmium, mercury, copper or silver
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/72Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44
    • C08F4/74Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals
    • C08F4/76Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals selected from titanium, zirconium, hafnium, vanadium, niobium or tantalum
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/72Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44
    • C08F4/74Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals
    • C08F4/78Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals selected from chromium, molybdenum or tungsten
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/72Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44
    • C08F4/80Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from iron group metals or platinum group metals

Definitions

  • the invention relates to a novel polymerization method of a vinyl monomer, in particular to a method for polymerizing a vinyl monomer by living polymerization by selecting an appropriate catalyst, an initiator and a solvent, and finally obtaining a molecular weight and a molecular weight.
  • a method of distributing a controllable polymer is a novel polymerization method of a vinyl monomer, in particular to a method for polymerizing a vinyl monomer by living polymerization by selecting an appropriate catalyst, an initiator and a solvent, and finally obtaining a molecular weight and a molecular weight.
  • the production methods of these polymers can be mainly divided into free radical polymerization, anionic (cationic) ion polymerization and coordination polymerization according to different reaction mechanisms.
  • the free radical polymerization has a wide range of suitable monomers, mild reaction conditions, and mature theoretical research, which is convenient for large-scale industrial production (Qiu Kunyuan. Polymer Bulletin, 2008(7): 15 The characteristics of -28), and thus the vinyl polymer produced by radical polymerization accounts for about 70% of the total yield of the vinyl polymer.
  • chain initiation is a key reaction that controls the rate of polymerization and the molecular weight of the polymer, directly affecting the polymerization rate of the monomer and the properties of the polymer.
  • the initiator of free radical polymerization can be divided into azo initiator, peroxide initiator, redox initiation system, etc. (Liu Yong, Huang Zhiyu, Lu Yi, et al. Chemical Journal, 2005, 19(3): 35 -39).
  • the azo initiator has no induced decomposition, is stable at normal temperature, and is convenient for storage and transportation, but its type is small, the applicable temperature range is narrow, and the price is high.
  • the peroxygen initiator is rich in products, low in price and wide in use, but the organic peroxide is generally low in purity, easy to react with other factors such as amines and alcohols in the polymerization system, and sensitive to heat, vibration and friction.
  • Storage and transportation troubles Jin Kegang, Xiao Jinping, Wang Huazhou. Fine Chemical Materials and Intermediates, 2007, (3): 18-20).
  • the redox-initiating system chain has low activation energy and can be polymerized at low temperature or room temperature, but the disadvantage is that the utilization efficiency of the initiator is low and the applicable temperature range is narrow.
  • active radical polymerization such as atom transfer radical polymerization (Wang J, Matyjaszewski K, J. Am. Chem.
  • the present invention does not use a radical polymerization initiator or an anion (cation) polymerization initiator, and does not use a coordination polymerization Zieg-Natta catalyst.
  • the polymerization method provided by the invention uses a transition metal nanoparticle as a catalyst and an organosilicon hydrogen compound as an initiator to initiate polymerization of a plurality of ethylenically unsaturated monomers, and finally obtains a controllable molecular weight and molecular weight distribution, and the terminal group contains Silicon polymer functional polymer.
  • the present invention adopts the following technical solutions:
  • a method for catalyzing a polymerization of a vinyl monomer by a transition metal nanoparticle the method being:
  • the monomer, catalyst, initiator and solvent are uniformly mixed and reacted at 0-130 ° C for 0.2-72 h, after which the reaction system is post-treated to obtain a product.
  • the monomer is an ethylenically unsaturated monomer; the catalyst is a transition metal nanoparticle; and the initiator is an organosilicon hydrogen compound.
  • the ratio of the amount of the monomer, the initiator, the catalyst, and the solvent to be charged is 1.0:0.0002 to 0.3:0.0000003 to 0.01:0 to 20, preferably 1:0.001 to 0.1:0.000001 to 0.001:0 to 1, particularly preferably 1:0.001 to 0.01: 0.0001 to 0.001: 0 to 0.5; wherein when the solvent is supplied at a ratio of 0, the monomer is directly subjected to bulk polymerization in the absence of a solvent.
  • a preferred reaction temperature is from 50 to 100 °C.
  • the preferred reaction time is from 1 to 36 hours.
  • the inert gas is, for example, one or a mixture of two or more of the following gases: nitrogen, argon, helium, neon.
  • the post-treatment of the reaction system may be carried out by conventional means known in the art. For example, after the reaction is completed, the reaction system is returned to normal temperature (20 to 30 ° C), and the reaction liquid is poured out or the solid substance is directly taken out to be a polymerization product. The final product is obtained by centrifuging, precipitating, grading, and conventional processing such as injection molding and molding.
  • the polymerization product obtained by the process of the present invention has a terminal group containing a silicone functional group, and the molecular weight and molecular weight distribution are controllable.
  • the molecular weight of the polymerization product is generally between 1.0 x 10 4 and 1.0 x 10 7 daltons, preferably between 5.0 x 10 4 and 5 x 10 6 daltons.
  • the molecular weight distribution of the polymerization product is generally between 1.2 and 3.0, preferably in the range of 1.3 to 2.0, depending on the molecular weight polydispersity index (PDI).
  • the monomer in the present invention is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
  • styrene including styrene, p-chloromethylstyrene, ⁇ -methylstyrene, p-fluorostyrene, p-chlorostyrene, p-bromostyrene, p-trifluoromethylstyrene, p-pair Vinylbenzene
  • Methacrylates including methyl methacrylate, ethyl methacrylate, propyl methacrylate, isopropyl methacrylate, butyl methacrylate, isobutyl methacrylate, methyl Octyl acrylate, isooctyl methacrylate, lauryl methacrylate, phenyl methacrylate, glycidyl methacrylate, triethylene glycol methacrylate, 2-ethyl methacrylate Ester, isobornyl methacrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, hydroxybutyl methacrylate, trifluoroethyl methacrylate, hexafluorobutyl methacrylate, N, N- Dimethylaminoethyl methacrylate, N,N-diethylaminoethyl methacrylate, 1,4-butylene glycol dimethacrylate;
  • (meth)acrylamides including acrylamide, methacrylamide, N-isopropylacrylamide, N-methylol acrylamide, N-(2-hydroxypropyl)methacrylamide, N-methacrylamide, N,N-dimethylacrylamide, N-tert-butylacrylamide, N-n-butylacrylamide, methylenebisacrylamide;
  • vinyl esters including vinyl acetate, vinyl chloroacetate, vinyl propionate, vinyl butyrate;
  • the monomer is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
  • styrenes including styrene, p-chloromethylstyrene, p-chlorostyrene
  • Methacrylates including methyl methacrylate, butyl methacrylate, lauryl methacrylate, 2-ethylhexyl methacrylate, glycidyl methacrylate, methacrylic acid Borneol ester, trifluoroethyl methacrylate, hexafluorobutyl methacrylate;
  • acrylates including methyl acrylate, ethyl acrylate, butyl acrylate, lauryl acrylate, hydroxyethyl acrylate, glycidyl acrylate, hexafluorobutyl acrylate;
  • (meth)acrylamides including acrylamide, methacrylamide, N-isopropylacrylamide, N-methylolacrylamide, N,N-dimethylacrylamide, methylene double Acrylamide;
  • vinyl esters including vinyl acetate, vinyl chloroacetate, vinyl propionate
  • the monomer is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
  • Styrene p-chloromethylstyrene, methyl methacrylate, butyl methacrylate, lauryl methacrylate, glycidyl methacrylate, isobornyl methacrylate, trifluoroethyl methacrylate , methyl acrylate, butyl acrylate, lauryl acrylate, hydroxyethyl acrylate, glycidyl acrylate, acrylamide, methacrylamide, N-isopropyl acrylamide, vinyl acetate, vinyl chloroacetate, propylene Nitrile, acrylic acid, 4-vinyl pyridine, N-vinyl pyrrolidone, vinyl chloride, isoprene.
  • the catalyst in the present invention is one or a mixture of two or more of the following transition metal nanoparticles: gold nanoparticles, silver nanoparticles, copper nanoparticles, platinum nanoparticles, palladium nanoparticles, nickel nanoparticles, ruthenium Nanoparticles, cerium nanoparticles, cerium nanoparticles, iron nanoparticles, cobalt nanoparticles, cerium nanoparticles, tungsten nanoparticles, titanium nanoparticles, vanadium nanoparticles, manganese nanoparticles, molybdenum nanoparticles, chromium nanoparticles.
  • Preferred catalysts are: gold nanoparticles, silver nanoparticles, copper nanoparticles, platinum nanoparticles, palladium nanoparticles, ruthenium nanoparticles, nickel nanoparticles, cobalt nanoparticles, ruthenium nanoparticles, titanium nanoparticles, molybdenum nanoparticles, chromium nanoparticles Particles, tungsten nanoparticles.
  • catalysts are: gold nanoparticles, silver nanoparticles, copper nanoparticles, platinum nanoparticles, palladium nanoparticles, molybdenum nanoparticles, tungsten nanoparticles.
  • the transition metal nanoparticles have an average particle diameter of between 1 and 100 nm, preferably between 2 and 20 nm.
  • the transition metal nanoparticles may be present in the form of a solid powder, a nanoparticle solution, or a nanoparticle loaded onto the surface of the solid substrate.
  • the solvent in the nanoparticle solution includes, but is not limited to, one or more of the following solvents: a mixture of any solvent in a miscible solvent: petroleum ether, n-hexane, toluene, chloroform, tetrahydrofuran, dioxane, and Phenyl ether, ethyl acetate, methanol, ethanol, water, aqueous PBS.
  • the material of the solid substrate includes, but is not limited to, one or a mixture of two or more of the following materials: activated carbon, aluminum oxide, silica gel, molecular sieve, calcium carbonate, barium sulfate, specifically, for example, palladium nanoparticles are loaded to Activated carbon (Pd/C).
  • the initiator in the present invention is one or a mixture of two or more of the following organosilicon compounds:
  • a trihydrosilane compound including phenylsilane, n-butylsilane, n-hexylsilane, cyclohexylsilane, n-octadecylsilane;
  • Dihydrosilane compounds including diphenylsilane, dipropylsilane, diisopropylsilane, di-n-butylsilane, diisobutylsilane, di-tert-butylsilane, di-n-hexylsilane, and Cyclohexylsilane, methylphenylsilane, phenylchlorosilane;
  • monohydrogen silane compounds including triphenyl silane, triethyl silane, tripropyl silane, triisopropyl silane, tri-n-butyl silane, triisobutyl silane, tri-tert-butyl silane, three N-hexylsilane, tricyclohexylsilane, tri-n-octylsilane, n-butyldimethylsilane, isobutyldimethylsilane, tert-butyldimethylsilane, tris(trimethylsilyl)silane, three (triethylsilyl)silane, trichlorosilane, methyldichlorosilane, ethyldichlorosilane, phenyldichlorosilane, dimethylchlorosilane, diphenylchlorosilane, diisopropylchlorosilane, Di-tert-but
  • the initiator is one or a mixture of two or more of the following organosilicon compounds:
  • a trihydrosilane compound including phenylsilane, n-hexylsilane;
  • dihydrosilane compound including diphenylsilane, diethylsilane, di-n-butylsilane, methylphenylsilane, phenylchlorosilane;
  • monohydrosilane compounds including triphenylsilane, triethylsilane, triisopropylsilane, tri-tert-butylsilane, tris(trimethylsilyl)silane, tris(triethylsilyl) Silane, trichlorosilane, methyldichlorosilane, phenyldichlorosilane, dimethylchlorosilane, diphenylchlorosilane, dimethylallylsilane, trimethoxysilane, triethoxysilane, three Tert-butoxysilane.
  • the initiator is one or a mixture of two or more of the following organosilicon compounds: phenylsilane, n-hexylsilane, diphenylsilane, diethylsilane, phenylchlorosilane, three Phenylsilane, triethylsilane, tri-tert-butylsilane, tris(trimethylsilyl)silane, dimethylallylsilane, triethoxysilane.
  • organosilicon compounds phenylsilane, n-hexylsilane, diphenylsilane, diethylsilane, phenylchlorosilane, three Phenylsilane, triethylsilane, tri-tert-butylsilane, tris(trimethylsilyl)silane, dimethylallylsilane, triethoxysilane.
  • the solvent in the present invention is a mixture of one or more of the following solvents in any ratio: n-hexane, cyclohexane, petroleum ether, heptane, octane, benzene, toluene, p-xylene, ten Hydrogen naphthalene, dichloromethane, chloroform, carbon tetrachloride, trichloroethylene, tetrachloroethylene, diethyl ether, n-butyl ether, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, triethylene glycol Methyl ether, tetrahydrofuran, dioxane, diphenyl ether, acetone, acetylacetone, methyl ethyl ketone, cyclohexanone, ethyl acetate, propyl acetate, butyl acetate, methanol, ethanol, isopropanol,
  • the room temperature in the present invention is 20 to 30 °C.
  • styrene vinyl chloride
  • vinyl acetate vinyl acetate
  • (meth) acrylate monomers vinyl acetate
  • (meth) acrylamide monomers 4-vinyl pyridine
  • N-ethylene a variety of monomers such as pyrrolidone
  • the reaction can be carried out at normal pressure, room temperature or near room temperature, and the amount of the catalyst can be as low as 1.0 ppm or less, no special equipment is required, the preparation steps are simple, and the production cost is low;
  • ultra-high molecular weight polymers with a molecular weight of more than 3 million. It is suitable for the production of high-strength and high-modulus polymer materials. It is used in chemical fiber, rubber elastomer, plastics, coatings, adhesives, biomedical polymers, etc. The prospects are very broad.
  • Figure 1a TEM image of gold nanoparticles in Example 1;
  • Figure 3 Example of gold particles in the resultant catalyst of MMA 1 PMMA and PDI- M n versus conversion
  • Figure 4a TEM image of Pd/C nanoparticles in Example 7;
  • Figure 5 Nuclear magnetic resonance ( 1 H-NMR) spectrum of PMMA obtained by catalytic polymerization of gold nanoparticles in Example 18.
  • Gold nanopowder organic solvent dispersible, average particle size 6nm, J&K Chemical
  • gold nanoparticle 0.1 mM PBS solution average particle size 20 nm, optical density value 1, Sigma-Aldrich
  • gold nanoparticle n-hexane solution average particle 4.1 nm, 0.75 mg/mL, reference Robinson I, Tung L D, Maenosono S, et al.
  • Nanoscale, 2010, 2, 2624-2630 platinum carbon (Pt/C, 5%, Aladdin), palladium Carbon (Pd/C, 5%, Aladdin), hydrogen (Ru/C, 5%, Aladdin), hydrogen (Rh/C, 5%, Aladdin), hydrogen (Ir/C, 5%, Macklin) , nano nickel powder (Ni, APS 10-25nm, Alfa Aesar), nano iron powder (Fe, APS 10-30nm, Alfa Aesar), nano copper powder (Cu, 99.9%, 10-30nm, Aladdin), nano silver powder ( Ag, APS 20-40 nm, Alfa Aesar), nano titanium powder (Ti, 99.8%, average particle size 60 nm, Aladdin), nano tungsten powder (W, 99.9%, average particle size 100 nm, Aladdin).
  • Tris(trimethylsilyl)silane TTSS, 97%, Sigma-Aldrich
  • tris(triethylsilyl)silane TTESS, 97%, Sigma-Aldrich
  • phenylsilane PSH, 98%, Alfa Aeser
  • Diphenylsilane DPS, 97%, Alfa Aeser
  • triphenylsilane TPS, 99%, Alfa Aeser
  • diethylsilane DES, 98%, Alfa Aeser
  • di-tert-butylsilane DTBS, 95%, TCI
  • triethylsilane TES, 97%, Alfa Aeser
  • triisopropylsilane TiPS, 99%, Alfa Aeser
  • methylphenylsilane MPS, 98%, Aldrich
  • II Benzylsilane DPMS, 97%, Alfa
  • triethoxysilane TEOS, 97%, Alfa
  • Styrene (St, 99%) and acrylamide (99%) were purchased from Alfa Aeser.
  • the monomers such as N-vinylpyrrolidone and isoprene are all Aladdin analytical reagents, and the column is treated with a basic Al 2 O 3 column before the reaction.
  • M n number average molecular weight
  • M w weight average molecular weight
  • PDI molecular weight distribution polydispersity coefficient
  • M PDI M w / M n
  • the measurement was performed by a permeation chromatography (GPC) system.
  • the system is equipped with Viscotek VE1122 solvent delivery unit, Viscotek VE 3580 refractive index detector, Viscotek 270 laser light scattering-differential viscometer dual detector, Viscotek VE2585 column oven and Viscotek T6000M GPC column.
  • M n , M w and PDI were measured using a Shimadzu Prominence GPC analysis system.
  • the system is equipped with Shimadzu RID-20A refractive index detector, Shimadzu SPD-15C UV visible light detector, Shimadzu LC-16C solvent delivery unit, Shimadzu CTO-16C column oven, and Waters Styragel HR 5E DMF column. .
  • Molecular weight calibration curves were prepared using a series of narrowly dispersed PMMA standards (Polymer Laboratories), data acquisition analysis software: Labsolutions Essentia 5.82.
  • Test conditions mobile phase, N,N-dimethylformamide (containing 0.01 M LiBr); column temperature, 50 ° C; mobile phase flow rate, 0.3 mL/min.
  • the molecular weight of polyacrylamide was determined by the viscosity method in accordance with the national standard GB17514-2008.
  • the molecular weight of polyacrylic acid is determined by the viscosity method by reference to Zhao Chunfeng, Liu Kunyuan, Han Shuzhen. Journal of Beijing University of Chemical Technology, 2002, 29(1): 51-55.
  • the nuclear magnetic resonance spectrum of the polymer material was measured on a Bruker Avance III 500 MHz NMR spectrometer.
  • the particle diameter of the metal nanoparticles was measured by a FEI Tecnai G2F30 high resolution transmission electron microscope (TEM).
  • the gold nanoparticle content in the n-hexane solution was measured by PerkinElmer ELAN DRC-e inductively coupled plasma mass spectrometer (ICP-MS). The conversion of the monomer during the reaction was determined gravimetrically.
  • the gold nanoparticle n-hexane solution prepared according to the reference was tested by transmission electron microscopy (TEM).
  • TEM transmission electron microscopy
  • EDX X-ray energy spectrum
  • Fig. 1 the gold nanoparticles are spherical. It has good dispersibility, a particle size of about 3 to 7 nm, and a statistical average particle diameter of 4.1 nm.
  • the gold content in the n-hexane solution was 0.75 mg/mL as measured by ICP-MS.
  • Fig. 2 It can be seen from Fig. 2 that the rate of polymerization of MMA by gold nanoparticles is very high. As the reaction time increases, the monomer conversion rate increases rapidly. The conversion rate is 13.0% at 50 min and 71.1% at 160 min. PMMA polymer has a number average molecular weight M n linearly increased from 1.6 ⁇ 10 5 5.0 ⁇ 10 5, PDI of the polymer is maintained at 2.7 or less (FIG. 3) increasing with conversion, the polymerization reaction exhibit living polymerization wherein The experimental operator can thereby control the molecular weight and molecular weight distribution of the polymerization product by changing the conversion rate of the polymerization reaction.
  • the 2.0 nm (1.01 ⁇ 10 -5 mol Au) organic solvent was added to the Schlenk reaction flask to disperse the gold nanopowder, vacuumed and filled with nitrogen, and 2 mL (0.019 mol) of pre-nitrogen-deoxygenated MMA monomer was added by syringe to ultrasonically oscillate. 1 min, stirring was started, then 10 ⁇ L (5.38 ⁇ 10 -5 mol) DPS was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 4.5 h. The reaction was stopped and the monomer conversion was 85.2%.
  • PMMA The weight average molecular weight was 2.96 million, the number average molecular weight was 1.31 million, and PDI was 2.25.
  • the purchased Pd/C powder catalyst was tested by transmission electron microscopy (TEM).
  • TEM transmission electron microscopy
  • EDX X-ray energy spectrum
  • Fig. 4 As can be seen from the figure, the Pd nanoparticles are spherical and uniformly dispersed.
  • the particle diameter was between 1-3 nm, and the statistical average particle diameter was 1.7 nm.
  • the polymer solution after the reaction was precipitated with methanol, and the obtained PMMA had a weight average molecular weight of 32,000, a number average molecular weight of 17,000, and a PDI of 1.88 as measured by GPC.
  • the nuclear magnetic resonance spectrum of the obtained PMMA is shown in Fig. 5.
  • the ratio of the PMMA polymer was calculated to be 16,000, which is consistent with the GPC measurement, indicating that a silicon-containing DPS initiator group is present at the end of each macromolecular chain.
  • This functional group can be further converted into other functional groups to obtain a more valuable functional polymer.
  • the conversion of the monomer was 85.1%
  • the weight average molecular weight of the poly(trifluoroethyl methacrylate) was 990,000
  • the number average molecular weight was 780,000
  • the PDI was 1.27.
  • the reaction was stopped after reacting at 90 ° C for 18 h.
  • the conversion of the monomer was 43.2%
  • the weight average molecular weight of poly(N-vinylpyrrolidone) was 470,000
  • the number average molecular weight was 180,000
  • PDI was 2.61.
  • PSH was stirred at room temperature for 5 min, then heated to 70 ° C for 39.5 h, and the reaction was stopped.
  • the conversion of the monomer was 56.8%
  • the weight average molecular weight of the copolymer was 450,000
  • the number average molecular weight was 154,000
  • PDI was 2.92.
  • Initiator azobisisobutyronitrile, azobisisovaleronitrile, azobisisoheptanenitrile, the amount of 0.6-2.0 wt%;
  • Polymer number average molecular weight 2772-14656; molecular weight distribution polydispersity index: 3.66-174.42.
  • the conventional radical polymerization initiator is used in a large amount, the obtained polymer has a low molecular weight, and the molecular weight distribution has a large polydispersity coefficient.
  • Monomer methyl methacrylate, concentration 1.23mol / L;
  • Initiator n-butyl lithium, concentration: 2.55 ⁇ 10 -2 mol / L;
  • reaction temperature -40 ° C
  • reaction in a sealed tube reaction time: 90 minutes
  • the anionic polymerization reaction condition of methyl methacrylate is severe, n-butyl lithium is extremely active, and it is required to carry out the reaction under low temperature conditions under a completely anhydrous condition, and the obtained polymer has a wide molecular weight distribution. , showing a bimodal distribution.
  • Monomer methyl methacrylate, concentration 10vol%
  • Catalyst Zieg-Natta catalyst TiCl 4 + AlEt 3 ;
  • reaction temperature -78 ° C
  • reaction time 18 h
  • the coordination polymerization conditions of methyl methacrylate are severe, and TiCl 4 and AlEt 3 are extremely active, and it is required to carry out the reaction in an extremely low temperature environment under completely anhydrous conditions, and the molecular weight of the obtained polymer is relatively high. low.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

The present invention provides a method for catalyzing polymerization of vinyl monomers by means of transition metal nanoparticles. The method comprises: uniformly mixing vinyl unsaturated monomers, the catalyst transition metal nanoparticles, an initiator organosilicon hydrogen compound and a solvent under the protection of an inert gas; performing reaction at 0 to 130 °C for 0.2 to 72 h; and then performing post-treatment of the reaction system, so as to obtain a product. The method of the present invention is suitable for a wide range of monomers, the reaction can be performed at or near room temperature and under a normal pressure, and the usage amount of the catalyst can be as low as 1.0 ppm or less, without the need for special equipment, the preparation process being simple, and the production cost being low. The method can produce ultra-high molecular weight polymers having a molecular weight of 3 million or more, being suitable for the production of high strength and high modulus polymer materials, having wide application prospects in the fields of chemical fibers, rubber elastomers, plastics, coatings, adhesives, biomedical polymers and the like.

Description

过渡金属纳米颗粒催化乙烯基单体聚合反应的方法Method for catalyzing polymerization of vinyl monomer by transition metal nanoparticles (一)技术领域(1) Technical field
本发明涉及一种乙烯基单体的聚合新方法,具体涉及一种通过选择适当的催化剂、引发剂和溶剂,可以使乙烯基单体以活性聚合的方式进行聚合反应,最终制得分子量和分子量分布可控的聚合物的方法。The invention relates to a novel polymerization method of a vinyl monomer, in particular to a method for polymerizing a vinyl monomer by living polymerization by selecting an appropriate catalyst, an initiator and a solvent, and finally obtaining a molecular weight and a molecular weight. A method of distributing a controllable polymer.
(二)背景技术(2) Background technology
全球每年生产逾两亿吨乙烯基聚合物,这些聚合物的生产方法按反应机理不同主要可分为自由基聚合、阴(阳)离子聚合和配位聚合。相对于阴(阳)离子聚合和配位聚合,自由基聚合具有适用单体范围广,反应条件温和,相关理论研究成熟,便于大规模工业化生产(丘坤元.高分子通报,2008(7):15-28)的特点,因而利用自由基聚合生产的乙烯基聚合物占乙烯基聚合物总产量的70%左右。The world produces more than 200 million tons of vinyl polymer per year. The production methods of these polymers can be mainly divided into free radical polymerization, anionic (cationic) ion polymerization and coordination polymerization according to different reaction mechanisms. Compared with the cation (cationic) ion polymerization and coordination polymerization, the free radical polymerization has a wide range of suitable monomers, mild reaction conditions, and mature theoretical research, which is convenient for large-scale industrial production (Qiu Kunyuan. Polymer Bulletin, 2008(7): 15 The characteristics of -28), and thus the vinyl polymer produced by radical polymerization accounts for about 70% of the total yield of the vinyl polymer.
自由基聚合中,链引发是控制聚合速率和聚合物分子量的关键反应,直接影响到单体的聚合速率和聚合物的性能。自由基聚合的引发剂可分为偶氮类引发剂、过氧化物类引发剂、氧化还原引发体系等(刘勇,黄志宇,陆屹,等.化工时刊,2005,19(3):35-39)。其中偶氮类引发剂无诱导分解,常温下较稳定,方便贮存和运输,但其种类较少,适用温度范围较窄,价格较高。过氧类引发剂产品丰富,价格较低廉,使用范围较广,但有机过氧化物一般纯度较低,易与聚合体系中的如胺、醇等发生副反应,而且对热、振动、摩擦敏感,贮存和运输麻烦(金可刚,肖锦平,王华周.精细化工原料及中间体,2007,(3):18-20)。氧化还原引发体系链引发活化能低,可在低温或室温聚合,但不足之处是引发剂的利用效率较低,适用温度范围窄。近年来出现的如原子转移自由基聚合(Wang J,Matyjaszewski K,J.Am.Chem.Soc.,1995,117:5614-5615.)、可逆加成断裂链转移聚合等活性自由基聚合(Le T P,Moad G,Rizzardo E,PCT Int.Appl.,WO 9801478A1,980115,1998)已在实验室中得到了普遍应用,但由于存在过渡金属络合物以及双硫酯链转移剂使用量大,成本较高,还需解决聚合物中的过渡金属络合物及双硫酯片段残留的问题而难以实现大规模工业化生产应用。In free radical polymerization, chain initiation is a key reaction that controls the rate of polymerization and the molecular weight of the polymer, directly affecting the polymerization rate of the monomer and the properties of the polymer. The initiator of free radical polymerization can be divided into azo initiator, peroxide initiator, redox initiation system, etc. (Liu Yong, Huang Zhiyu, Lu Yi, et al. Chemical Journal, 2005, 19(3): 35 -39). Among them, the azo initiator has no induced decomposition, is stable at normal temperature, and is convenient for storage and transportation, but its type is small, the applicable temperature range is narrow, and the price is high. The peroxygen initiator is rich in products, low in price and wide in use, but the organic peroxide is generally low in purity, easy to react with other factors such as amines and alcohols in the polymerization system, and sensitive to heat, vibration and friction. Storage and transportation troubles (Jin Kegang, Xiao Jinping, Wang Huazhou. Fine Chemical Materials and Intermediates, 2007, (3): 18-20). The redox-initiating system chain has low activation energy and can be polymerized at low temperature or room temperature, but the disadvantage is that the utilization efficiency of the initiator is low and the applicable temperature range is narrow. In recent years, active radical polymerization such as atom transfer radical polymerization (Wang J, Matyjaszewski K, J. Am. Chem. Soc., 1995, 117: 5614-5615.), reversible addition fragmentation chain transfer polymerization (Le T P, Moad G, Rizzardo E, PCT Int. Appl., WO 9801478A1, 980115, 1998) have been widely used in the laboratory, but due to the large amount of transition metal complexes and dithioester chain transfer agents. The cost is high, and the problem of transition metal complexes and dithioester fragments remaining in the polymer needs to be solved, and it is difficult to realize large-scale industrial production applications.
(三)发明内容(3) Invention content
本发明目的是提供一种新的乙烯基单体的聚合方法。区别于传统自由基聚合、阴(阳)离子聚合或配位聚合方法,本发明不使用自由基聚合引发剂或阴(阳)离子聚合引发剂,也不使用配位聚合齐格-纳塔催化剂,本发明提供的聚合方法以过渡金属纳米颗粒为催化剂,以有机硅氢化合物为引发剂,引发多种乙烯基不饱和单体进行聚合反应,最终制得分子量和分子量分布可控、端基含有机硅官能团的高分子聚合物。It is an object of the present invention to provide a novel polymerization process for vinyl monomers. Different from the conventional radical polymerization, anion (cation) polymerization or coordination polymerization method, the present invention does not use a radical polymerization initiator or an anion (cation) polymerization initiator, and does not use a coordination polymerization Zieg-Natta catalyst. The polymerization method provided by the invention uses a transition metal nanoparticle as a catalyst and an organosilicon hydrogen compound as an initiator to initiate polymerization of a plurality of ethylenically unsaturated monomers, and finally obtains a controllable molecular weight and molecular weight distribution, and the terminal group contains Silicon polymer functional polymer.
为实现上述目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,所述的方法为:A method for catalyzing a polymerization of a vinyl monomer by a transition metal nanoparticle, the method being:
在惰性气体保护下,将单体、催化剂、引发剂、溶剂混合均匀,于0~130℃下反应0.2~72h,之后反应体系经后处理,即得产品。Under the protection of inert gas, the monomer, catalyst, initiator and solvent are uniformly mixed and reacted at 0-130 ° C for 0.2-72 h, after which the reaction system is post-treated to obtain a product.
所述单体为乙烯基不饱和单体;所述催化剂为过渡金属纳米颗粒;所述引发剂为有机硅氢化合物。The monomer is an ethylenically unsaturated monomer; the catalyst is a transition metal nanoparticle; and the initiator is an organosilicon hydrogen compound.
所述单体、引发剂、催化剂、溶剂的投料物质的量之比为1.0:0.0002~0.3:0.0000003~0.01:0~20,优选1:0.001~0.1:0.000001~0.001:0~1,特别优选1:0.001~0.01:0.0001~0.001:0~0.5;其中,所述溶剂的投料比例为0时,则单体在无溶剂情况直接进行本体聚合反应。The ratio of the amount of the monomer, the initiator, the catalyst, and the solvent to be charged is 1.0:0.0002 to 0.3:0.0000003 to 0.01:0 to 20, preferably 1:0.001 to 0.1:0.000001 to 0.001:0 to 1, particularly preferably 1:0.001 to 0.01: 0.0001 to 0.001: 0 to 0.5; wherein when the solvent is supplied at a ratio of 0, the monomer is directly subjected to bulk polymerization in the absence of a solvent.
优选的反应温度为50~100℃。A preferred reaction temperature is from 50 to 100 °C.
优选的反应时间为1~36h。The preferred reaction time is from 1 to 36 hours.
所述的惰性气体例如下列气体中的一种或两种以上任意比例的混合:氮气、氩气、氦气、氖气。The inert gas is, for example, one or a mixture of two or more of the following gases: nitrogen, argon, helium, neon.
所述反应体系的后处理可采用本领域公知的常规手段,例如:反应结束后,待反应体系恢复至常温(20~30℃),倾倒出反应液或直接取出固体物质即为聚合产物,进一步对聚合产物进行离心、沉淀、分级以及注塑、成模等常规加工处理,即得最终产品。The post-treatment of the reaction system may be carried out by conventional means known in the art. For example, after the reaction is completed, the reaction system is returned to normal temperature (20 to 30 ° C), and the reaction liquid is poured out or the solid substance is directly taken out to be a polymerization product. The final product is obtained by centrifuging, precipitating, grading, and conventional processing such as injection molding and molding.
按照本发明方法制得的聚合产物,其端基含有机硅官能团,分子量以及分子量分布可控。所述聚合产物的分子量一般介于1.0×10 4~1.0×10 7道尔顿之间,优选介于5.0×10 4~5×10 6道尔顿之间。所述聚合产物的分子量分布,根据分子量多分散指数(PDI)的大小,一般介于1.2~3.0之间,优选PDI范围为1.3~2.0。 The polymerization product obtained by the process of the present invention has a terminal group containing a silicone functional group, and the molecular weight and molecular weight distribution are controllable. The molecular weight of the polymerization product is generally between 1.0 x 10 4 and 1.0 x 10 7 daltons, preferably between 5.0 x 10 4 and 5 x 10 6 daltons. The molecular weight distribution of the polymerization product is generally between 1.2 and 3.0, preferably in the range of 1.3 to 2.0, depending on the molecular weight polydispersity index (PDI).
本发明中所述单体为下列单体中的一种,或者两种以上可以互溶单体的任意比例混合物:The monomer in the present invention is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
(1)苯乙烯类,包括苯乙烯、对氯甲基苯乙烯、α-甲基苯乙烯、对氟苯乙烯、对氯苯乙烯、对溴苯乙烯、对三氟甲基苯乙烯、对二乙烯基苯;(1) styrene, including styrene, p-chloromethylstyrene, α-methylstyrene, p-fluorostyrene, p-chlorostyrene, p-bromostyrene, p-trifluoromethylstyrene, p-pair Vinylbenzene
(2)甲基丙烯酸酯类,包括甲基丙烯酸甲酯、甲基丙烯酸乙酯、甲基丙烯酸丙酯、甲基丙烯酸异丙酯、甲基丙烯酸丁酯、甲基丙烯酸异丁酯、甲基丙烯酸辛酯、甲基丙烯酸异辛酯、甲基丙烯酸月桂酯、甲基丙烯酸苯酯、甲基丙烯酸缩水甘油醚酯、二缩三乙二醇甲基丙烯酸酯、甲基丙烯酸2-乙基已酯、甲基丙烯酸异冰片酯、甲基丙烯酸羟乙酯、甲基丙烯酸羟丙酯、甲基丙烯酸羟丁酯、甲基丙烯酸三氟乙酯、甲基丙烯酸六氟丁酯、N,N-二甲胺基乙基甲基丙烯酸酯、N,N-二乙胺基乙基甲基丙烯酸酯、二甲基丙烯酸1,4-丁二醇酯;(2) Methacrylates, including methyl methacrylate, ethyl methacrylate, propyl methacrylate, isopropyl methacrylate, butyl methacrylate, isobutyl methacrylate, methyl Octyl acrylate, isooctyl methacrylate, lauryl methacrylate, phenyl methacrylate, glycidyl methacrylate, triethylene glycol methacrylate, 2-ethyl methacrylate Ester, isobornyl methacrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, hydroxybutyl methacrylate, trifluoroethyl methacrylate, hexafluorobutyl methacrylate, N, N- Dimethylaminoethyl methacrylate, N,N-diethylaminoethyl methacrylate, 1,4-butylene glycol dimethacrylate;
(3)丙烯酸酯类,包括丙烯酸甲酯、丙烯酸乙酯、丙烯酸丙酯、丙烯酸异丙酯、丙烯酸丁酯、丙烯酸异丁酯、丙烯酸辛酯、丙烯酸异辛酯、丙烯酸月桂酯、丙烯酸羟乙酯、丙烯酸羟丙酯及、丙烯酸羟丁酯、N,N-二甲胺基乙基丙烯酸酯、N,N-二乙胺基乙基丙烯酸酯、丙烯酸三氟乙酯、丙烯酸缩水甘油醚酯、二缩三乙二醇丙烯酸酯、丙烯酸六氟丁酯、丙烯酸2-乙基己酯、丙烯酸苯酯、二丙烯酸1,4-丁二醇酯、丙烯酸异冰片酯;(3) Acrylates, including methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate, isobutyl acrylate, octyl acrylate, isooctyl acrylate, lauryl acrylate, hydroxyethyl acrylate Ester, hydroxypropyl acrylate and hydroxybutyl acrylate, N,N-dimethylaminoethyl acrylate, N,N-diethylaminoethyl acrylate, trifluoroethyl acrylate, glycidyl acrylate , triethylene glycol acrylate, hexafluorobutyl acrylate, 2-ethylhexyl acrylate, phenyl acrylate, 1,4-butylene glycol diacrylate, isobornyl acrylate;
(4)(甲基)丙烯酰胺类,包括丙烯酰胺、甲基丙烯酰胺、N-异丙基丙烯酰胺、N-羟甲基丙烯酰胺、N-(2-羟丙基)甲基丙烯酰胺、N-甲基丙烯酰胺、N,N-二甲基丙烯酰胺、N-特丁基丙烯酰胺、N-正丁基丙烯酰胺、亚甲基双丙烯酰胺;(4) (meth)acrylamides, including acrylamide, methacrylamide, N-isopropylacrylamide, N-methylol acrylamide, N-(2-hydroxypropyl)methacrylamide, N-methacrylamide, N,N-dimethylacrylamide, N-tert-butylacrylamide, N-n-butylacrylamide, methylenebisacrylamide;
(5)乙烯酯类,包括醋酸乙烯酯、氯乙酸乙烯酯、丙酸乙烯酯、丁酸乙烯酯;(5) vinyl esters, including vinyl acetate, vinyl chloroacetate, vinyl propionate, vinyl butyrate;
(6)其它类别单体,包括丙烯腈、甲基丙烯腈、丙烯酸、甲基丙烯酸、4-乙烯基吡啶、N-乙烯基吡咯烷酮、氯乙烯、异戊二烯、丁二烯。(6) Other types of monomers, including acrylonitrile, methacrylonitrile, acrylic acid, methacrylic acid, 4-vinylpyridine, N-vinylpyrrolidone, vinyl chloride, isoprene, butadiene.
优选的,所述单体为下列单体中的一种,或者两种以上可以互溶单体的任意比例混合物:Preferably, the monomer is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
(1)苯乙烯类,包括苯乙烯、对氯甲基苯乙烯、对氯苯乙烯;(1) styrenes, including styrene, p-chloromethylstyrene, p-chlorostyrene;
(2)甲基丙烯酸酯类,包括甲基丙烯酸甲酯、甲基丙烯酸丁酯、甲基丙烯酸月桂酯、甲 基丙烯酸2-乙基已酯、甲基丙烯酸缩水甘油醚酯、甲基丙烯酸异冰片酯、甲基丙烯酸三氟乙酯、甲基丙烯酸六氟丁酯;(2) Methacrylates, including methyl methacrylate, butyl methacrylate, lauryl methacrylate, 2-ethylhexyl methacrylate, glycidyl methacrylate, methacrylic acid Borneol ester, trifluoroethyl methacrylate, hexafluorobutyl methacrylate;
(3)丙烯酸酯类,包括丙烯酸甲酯、丙烯酸乙酯、丙烯酸丁酯、丙烯酸月桂酯、丙烯酸羟乙酯、丙烯酸缩水甘油醚酯、丙烯酸六氟丁酯;(3) acrylates, including methyl acrylate, ethyl acrylate, butyl acrylate, lauryl acrylate, hydroxyethyl acrylate, glycidyl acrylate, hexafluorobutyl acrylate;
(4)(甲基)丙烯酰胺类,包括丙烯酰胺、甲基丙烯酰胺、N-异丙基丙烯酰胺、N-羟甲基丙烯酰胺、N,N-二甲基丙烯酰胺、亚甲基双丙烯酰胺;(4) (meth)acrylamides, including acrylamide, methacrylamide, N-isopropylacrylamide, N-methylolacrylamide, N,N-dimethylacrylamide, methylene double Acrylamide;
(5)乙烯酯类,包括醋酸乙烯酯、氯乙酸乙烯酯、丙酸乙烯酯;(5) vinyl esters, including vinyl acetate, vinyl chloroacetate, vinyl propionate;
(6)其它类别单体,包括丙烯腈、丙烯酸、4-乙烯基吡啶、N-乙烯基吡咯烷酮、氯乙烯、异戊二烯。(6) Other types of monomers, including acrylonitrile, acrylic acid, 4-vinylpyridine, N-vinylpyrrolidone, vinyl chloride, isoprene.
特别优选的,所述单体为下列单体中的一种,或者两种以上可以互溶单体的任意比例混合物:Particularly preferably, the monomer is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
苯乙烯、对氯甲基苯乙烯、甲基丙烯酸甲酯、甲基丙烯酸丁酯、甲基丙烯酸月桂酯、甲基丙烯酸缩水甘油醚酯、甲基丙烯酸异冰片酯、甲基丙烯酸三氟乙酯、丙烯酸甲酯、丙烯酸丁酯、丙烯酸月桂酯、丙烯酸羟乙酯、丙烯酸缩水甘油醚酯、丙烯酰胺、甲基丙烯酰胺、N-异丙基丙烯酰胺、醋酸乙烯酯、氯乙酸乙烯酯、丙烯腈、丙烯酸、4-乙烯基吡啶、N-乙烯基吡咯烷酮、氯乙烯、异戊二烯。Styrene, p-chloromethylstyrene, methyl methacrylate, butyl methacrylate, lauryl methacrylate, glycidyl methacrylate, isobornyl methacrylate, trifluoroethyl methacrylate , methyl acrylate, butyl acrylate, lauryl acrylate, hydroxyethyl acrylate, glycidyl acrylate, acrylamide, methacrylamide, N-isopropyl acrylamide, vinyl acetate, vinyl chloroacetate, propylene Nitrile, acrylic acid, 4-vinyl pyridine, N-vinyl pyrrolidone, vinyl chloride, isoprene.
本发明中所述催化剂为下列过渡金属纳米颗粒中的一种或两种以上任意比例的混合物:金纳米颗粒、银纳米颗粒、铜纳米颗粒、铂纳米颗粒、钯纳米颗粒、镍纳米颗粒、铑纳米颗粒、铼纳米颗粒、钌纳米颗粒、铁纳米颗粒、钴纳米颗粒、铱纳米颗粒、钨纳米颗粒、钛纳米颗粒、钒纳米颗粒、锰纳米颗粒、钼纳米颗粒、铬纳米颗粒。The catalyst in the present invention is one or a mixture of two or more of the following transition metal nanoparticles: gold nanoparticles, silver nanoparticles, copper nanoparticles, platinum nanoparticles, palladium nanoparticles, nickel nanoparticles, ruthenium Nanoparticles, cerium nanoparticles, cerium nanoparticles, iron nanoparticles, cobalt nanoparticles, cerium nanoparticles, tungsten nanoparticles, titanium nanoparticles, vanadium nanoparticles, manganese nanoparticles, molybdenum nanoparticles, chromium nanoparticles.
优选催化剂为:金纳米颗粒、银纳米颗粒、铜纳米颗粒、铂纳米颗粒、钯纳米颗粒、铑纳米颗粒、镍纳米颗粒、钴纳米颗粒、钌纳米颗粒、钛纳米颗粒、钼纳米颗粒、铬纳米颗粒、钨纳米颗粒。Preferred catalysts are: gold nanoparticles, silver nanoparticles, copper nanoparticles, platinum nanoparticles, palladium nanoparticles, ruthenium nanoparticles, nickel nanoparticles, cobalt nanoparticles, ruthenium nanoparticles, titanium nanoparticles, molybdenum nanoparticles, chromium nanoparticles Particles, tungsten nanoparticles.
特别优选催化剂为:金纳米颗粒、银纳米颗粒、铜纳米颗粒、铂纳米颗粒、钯纳米颗粒、钼纳米颗粒、钨纳米颗粒。Particularly preferred catalysts are: gold nanoparticles, silver nanoparticles, copper nanoparticles, platinum nanoparticles, palladium nanoparticles, molybdenum nanoparticles, tungsten nanoparticles.
所述过渡金属纳米颗粒的平均粒径在1~100nm之间,优选在2~20nm之间。所述过渡金属纳米颗粒的存在形式可以为固体粉末、纳米颗粒溶液或纳米颗粒负载到固体基质表面的形式。所述纳米颗粒溶液中的溶剂包括但不限于下列溶剂中的一种或两种以上可以互溶溶剂的任意比例混合物:石油醚、正己烷、甲苯、三氯甲烷、四氢呋喃、二氧六环、二苯醚、乙酸乙酯、甲醇、乙醇、水、PBS水溶液。所述固体基质的材料包括但不限于下列材料中的一种或两种以上任意比例的混合物:活性炭、三氧化二铝、硅胶、分子筛、碳酸钙、硫酸钡,具体例如,钯纳米颗粒负载到活性炭上(Pd/C)。The transition metal nanoparticles have an average particle diameter of between 1 and 100 nm, preferably between 2 and 20 nm. The transition metal nanoparticles may be present in the form of a solid powder, a nanoparticle solution, or a nanoparticle loaded onto the surface of the solid substrate. The solvent in the nanoparticle solution includes, but is not limited to, one or more of the following solvents: a mixture of any solvent in a miscible solvent: petroleum ether, n-hexane, toluene, chloroform, tetrahydrofuran, dioxane, and Phenyl ether, ethyl acetate, methanol, ethanol, water, aqueous PBS. The material of the solid substrate includes, but is not limited to, one or a mixture of two or more of the following materials: activated carbon, aluminum oxide, silica gel, molecular sieve, calcium carbonate, barium sulfate, specifically, for example, palladium nanoparticles are loaded to Activated carbon (Pd/C).
本发明中所述引发剂为下列有机硅氢化合物中的一种或两种以上任意比例的混合物:The initiator in the present invention is one or a mixture of two or more of the following organosilicon compounds:
(1)三氢硅烷类化合物,包括苯硅烷、正丁基硅烷、正己基硅烷、环己基硅烷、正十八烷基硅烷;(1) a trihydrosilane compound, including phenylsilane, n-butylsilane, n-hexylsilane, cyclohexylsilane, n-octadecylsilane;
(2)二氢硅烷类化合物,包括二苯基硅烷、二丙基硅烷、二异丙基硅烷、二正丁基硅烷、二异丁基硅烷、二叔丁基硅烷、二正己基硅烷、二环己基硅烷、甲基苯基硅烷、苯基氯硅烷;(2) Dihydrosilane compounds, including diphenylsilane, dipropylsilane, diisopropylsilane, di-n-butylsilane, diisobutylsilane, di-tert-butylsilane, di-n-hexylsilane, and Cyclohexylsilane, methylphenylsilane, phenylchlorosilane;
(3)单氢硅烷类化合物,包括三苯基硅烷、三乙基硅烷、三丙基硅烷、三异丙基硅烷、三正丁基硅烷、三异丁基硅烷、三叔丁基硅烷、三正己基硅烷、三环己基硅烷、三正辛基硅烷、正丁基二甲基硅烷、异丁基二甲基硅烷、叔丁基二甲基硅烷、三(三甲基硅基)硅烷、三(三乙基硅基)硅烷、三氯硅烷、甲基二氯硅烷、乙基二氯硅烷、苯基二氯硅烷、二甲基氯硅烷、二苯基氯硅烷、二异丙基氯硅烷、二叔丁基氯硅烷、甲基苯基氯硅烷、二甲基烯丙基硅烷、甲基二苯基硅烷、二甲基苯基硅烷、二甲基正己基硅烷、二甲基正丁基硅烷、正十八烷基二乙氧基硅烷、三甲氧基硅烷、三乙氧基硅烷、三丙氧基硅烷、三异丙氧基硅烷、三丁氧基硅烷、三叔丁氧基硅烷、甲基二甲氧基硅烷、甲基二乙氧基硅烷、苯基二甲氧基硅烷、苯基二乙氧基硅烷。(3) monohydrogen silane compounds, including triphenyl silane, triethyl silane, tripropyl silane, triisopropyl silane, tri-n-butyl silane, triisobutyl silane, tri-tert-butyl silane, three N-hexylsilane, tricyclohexylsilane, tri-n-octylsilane, n-butyldimethylsilane, isobutyldimethylsilane, tert-butyldimethylsilane, tris(trimethylsilyl)silane, three (triethylsilyl)silane, trichlorosilane, methyldichlorosilane, ethyldichlorosilane, phenyldichlorosilane, dimethylchlorosilane, diphenylchlorosilane, diisopropylchlorosilane, Di-tert-butylchlorosilane, methylphenylchlorosilane, dimethylallylsilane, methyldiphenylsilane, dimethylphenylsilane, dimethyl-n-hexylsilane, dimethyl-n-butylsilane , n-octadecyldiethoxysilane, trimethoxysilane, triethoxysilane, tripropoxysilane, triisopropoxysilane, tributoxysilane, tri-tert-butoxysilane, A Dimethoxysilane, methyldiethoxysilane, phenyldimethoxysilane, phenyldiethoxysilane.
优选的,所述引发剂为下列有机硅氢化合物中的一种或两种以上任意比例的混合物:Preferably, the initiator is one or a mixture of two or more of the following organosilicon compounds:
(1)三氢硅烷类化合物,包括苯硅烷、正己基硅烷;(1) a trihydrosilane compound, including phenylsilane, n-hexylsilane;
(2)二氢硅烷类化合物,包括二苯基硅烷、二乙基硅烷、二正丁基硅烷、甲基苯基硅烷、苯基氯硅烷;(2) a dihydrosilane compound, including diphenylsilane, diethylsilane, di-n-butylsilane, methylphenylsilane, phenylchlorosilane;
(3)单氢硅烷类化合物,包括三苯基硅烷、三乙基硅烷、三异丙基硅烷、三叔丁基硅烷、三(三甲基硅基)硅烷、三(三乙基硅基)硅烷、三氯硅烷、甲基二氯硅烷、苯基二氯硅烷、二甲基氯硅烷、二苯基氯硅烷、二甲基烯丙基硅烷、三甲氧基硅烷、三乙氧基硅烷、三叔丁氧基硅烷。(3) monohydrosilane compounds, including triphenylsilane, triethylsilane, triisopropylsilane, tri-tert-butylsilane, tris(trimethylsilyl)silane, tris(triethylsilyl) Silane, trichlorosilane, methyldichlorosilane, phenyldichlorosilane, dimethylchlorosilane, diphenylchlorosilane, dimethylallylsilane, trimethoxysilane, triethoxysilane, three Tert-butoxysilane.
特别优选的,所述引发剂为下列有机硅氢化合物中的一种或两种以上任意比例的混合物:苯硅烷、正己基硅烷、二苯基硅烷、二乙基硅烷、苯基氯硅烷、三苯基硅烷、三乙基硅烷、三叔丁基硅烷、三(三甲基硅基)硅烷、二甲基烯丙基硅烷、三乙氧基硅烷。Particularly preferably, the initiator is one or a mixture of two or more of the following organosilicon compounds: phenylsilane, n-hexylsilane, diphenylsilane, diethylsilane, phenylchlorosilane, three Phenylsilane, triethylsilane, tri-tert-butylsilane, tris(trimethylsilyl)silane, dimethylallylsilane, triethoxysilane.
本发明中所述溶剂为下列溶剂中的一种或两种以上可以互溶溶剂的任意比例混合物:正己烷、环己烷、石油醚、庚烷、辛烷、苯、甲苯、对二甲苯、十氢萘、二氯甲烷、三氯甲烷、四氯化碳、三氯乙烯、四氯乙烯、乙醚、正丁醚、乙二醇二甲醚、二乙二醇二甲醚、三乙二醇二甲醚、四氢呋喃、二氧六环、二苯醚、丙酮、乙酰丙酮、丁酮、环己酮、乙酸乙酯、乙酸丙酯、乙酸丁酯、甲醇、乙醇、异丙醇、正丁醇、异丁醇、环己醇、乙二醇、一缩二乙二醇、二缩三乙二醇、水、N,N-二甲基甲酰胺、N-甲基甲酰胺、N-甲基乙酰胺、二甲基亚砜、环丁砜、N-甲基吡咯烷酮、γ-丁内酯。The solvent in the present invention is a mixture of one or more of the following solvents in any ratio: n-hexane, cyclohexane, petroleum ether, heptane, octane, benzene, toluene, p-xylene, ten Hydrogen naphthalene, dichloromethane, chloroform, carbon tetrachloride, trichloroethylene, tetrachloroethylene, diethyl ether, n-butyl ether, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, triethylene glycol Methyl ether, tetrahydrofuran, dioxane, diphenyl ether, acetone, acetylacetone, methyl ethyl ketone, cyclohexanone, ethyl acetate, propyl acetate, butyl acetate, methanol, ethanol, isopropanol, n-butanol, Isobutanol, cyclohexanol, ethylene glycol, diethylene glycol, triethylene glycol, water, N,N-dimethylformamide, N-methylformamide, N-methyl Amide, dimethyl sulfoxide, sulfolane, N-methylpyrrolidone, γ-butyrolactone.
本发明中的室温为20~30℃。The room temperature in the present invention is 20 to 30 °C.
本发明具有三个明显的优势:The invention has three distinct advantages:
第一,适用单体范围很广,包括苯乙烯、氯乙烯、醋酸乙烯酯、(甲基)丙烯酸酯类单体、(甲基)丙烯酰胺类单体、4-乙烯基吡啶、N-乙烯基吡咯烷酮等多种单体;First, a wide range of suitable monomers, including styrene, vinyl chloride, vinyl acetate, (meth) acrylate monomers, (meth) acrylamide monomers, 4-vinyl pyridine, N-ethylene a variety of monomers such as pyrrolidone;
第二,反应可在常压、室温或室温附近进行,催化剂的使用量最低可低至1.0ppm以下,无需特殊的仪器设备,制备步骤简单,生产成本低廉;Secondly, the reaction can be carried out at normal pressure, room temperature or near room temperature, and the amount of the catalyst can be as low as 1.0 ppm or less, no special equipment is required, the preparation steps are simple, and the production cost is low;
第三,可制备分子量超过300万以上的超高分子量聚合物,适用于生产高强高模聚合物材料,在化学纤维、橡胶弹性体、塑料、涂料、粘胶剂、生物医用高分子等领域应用前景十分广泛。Third, it can prepare ultra-high molecular weight polymers with a molecular weight of more than 3 million. It is suitable for the production of high-strength and high-modulus polymer materials. It is used in chemical fiber, rubber elastomer, plastics, coatings, adhesives, biomedical polymers, etc. The prospects are very broad.
(四)附图说明(4) Description of the drawings
图1a:实施例1中金纳米粒子的TEM图像;Figure 1a: TEM image of gold nanoparticles in Example 1;
图1b:实施例1中金纳米粒子的EDX能谱图;Figure 1b: EDX spectrum of gold nanoparticles in Example 1;
图2:实施例1中金纳米粒子催化MMA聚合反应的转化率-时间关系曲线;Figure 2: Conversion rate-time curve of gold nanoparticle catalyzed MMA polymerization in Example 1;
图3:实施例1中金纳米粒子催化MMA所得PMMA的M n及PDI-转化率关系曲线; Figure 3: Example of gold particles in the resultant catalyst of MMA 1 PMMA and PDI- M n versus conversion;
图4a:实施例7中Pd/C纳米粒子的TEM图像;Figure 4a: TEM image of Pd/C nanoparticles in Example 7;
图4b:实施例7中Pd/C纳米粒子的EDX能谱图;Figure 4b: EDX spectrum of Pd/C nanoparticles in Example 7;
图5:实施例18中金纳米粒子催化MMA聚合所得PMMA的核磁共振( 1H-NMR)谱图。 Figure 5: Nuclear magnetic resonance ( 1 H-NMR) spectrum of PMMA obtained by catalytic polymerization of gold nanoparticles in Example 18.
(五)具体实施方式(5) Specific implementation methods
下面通过具体实施例来进一步说明本发明的目的、优点和技术方案的实施细节。由于同类单体或同类引发剂的性质相似,在实施例中仅使用该类单体或引发剂中的典型代表(如苯乙烯类单体中的苯乙烯、甲基丙烯酸酯类单体中的甲基丙烯酸甲酯与甲基丙烯酸异冰片酯、丙烯酸酯类单体中的丙烯酸甲酯与丙烯酸丁酯,三氢硅烷类引发剂中的苯硅烷等等)来进行举例说明。实施例中列举的具体物质和用量以及其它细节条件不构成对本发明的限制。本领域的技术人员根据本发明可以设计出许多其它的修改形式和实施例,这些修改形式和实施例也属于本发明的范畴。The details of the objects, advantages and technical solutions of the present invention are further illustrated by the specific embodiments. Due to the similar nature of similar monomers or similar initiators, only typical examples of such monomers or initiators are used in the examples (eg, in styrene, methacrylate monomers in styrenic monomers). Methyl methacrylate and isobornyl methacrylate, methyl acrylate and butyl acrylate in acrylate monomers, phenyl silane in a trihydrosilane initiator, and the like are exemplified. The specific materials and amounts and other details set forth in the examples are not intended to limit the invention. Many other modifications and embodiments can be devised by those skilled in the art in light of the present invention. These modifications and embodiments are also within the scope of the invention.
在具体实施实例过程中所用原材料、仪器设备以及测试表征方法如下。The raw materials, equipment, and test characterization methods used in the specific example process are as follows.
试剂材料Reagent material
金纳米粉末(有机溶剂可分散,平均粒径6nm,J&K Chemical),金纳米粒子0.1mM PBS溶液(平均粒径20nm,光密度值1,Sigma-Aldrich),金纳米粒子正己烷溶液(平均粒径4.1nm,0.75mg/mL,参照文献Robinson I,Tung L D,Maenosono S,et al.Nanoscale,2010,2,2624-2630自制),铂碳(Pt/C,5%,Aladdin),钯碳(Pd/C,5%,Aladdin),钌碳(Ru/C,5%,Aladdin),铑碳(Rh/C,5%,Aladdin),铱碳(Ir/C,5%,Macklin),纳米镍粉(Ni,APS 10-25nm,Alfa Aesar),纳米铁粉(Fe,APS 10-30nm,Alfa Aesar),纳米铜粉(Cu,99.9%,10-30nm,Aladdin),纳米银粉(Ag,APS 20-40nm,Alfa Aesar),纳米钛粉(Ti,99.8%,平均粒径60nm,Aladdin),纳米钨粉(W,99.9%,平均粒径100nm,Aladdin)。Gold nanopowder (organic solvent dispersible, average particle size 6nm, J&K Chemical), gold nanoparticle 0.1 mM PBS solution (average particle size 20 nm, optical density value 1, Sigma-Aldrich), gold nanoparticle n-hexane solution (average particle 4.1 nm, 0.75 mg/mL, reference Robinson I, Tung L D, Maenosono S, et al. Nanoscale, 2010, 2, 2624-2630), platinum carbon (Pt/C, 5%, Aladdin), palladium Carbon (Pd/C, 5%, Aladdin), hydrogen (Ru/C, 5%, Aladdin), hydrogen (Rh/C, 5%, Aladdin), hydrogen (Ir/C, 5%, Macklin) , nano nickel powder (Ni, APS 10-25nm, Alfa Aesar), nano iron powder (Fe, APS 10-30nm, Alfa Aesar), nano copper powder (Cu, 99.9%, 10-30nm, Aladdin), nano silver powder ( Ag, APS 20-40 nm, Alfa Aesar), nano titanium powder (Ti, 99.8%, average particle size 60 nm, Aladdin), nano tungsten powder (W, 99.9%, average particle size 100 nm, Aladdin).
三(三甲硅基)硅烷(TTSS,97%,Sigma-Aldrich),三(三乙基硅)硅烷(TTESS,97%,Sigma-Aldrich),苯基硅烷(PSH,98%,Alfa Aeser),二苯基硅烷(DPS,97%,Alfa Aeser),三苯基硅烷(TPS,99%,Alfa Aeser),二乙基硅烷(DES,98%,Alfa Aeser),二叔丁基硅烷(DTBS,95%,TCI),三乙基硅烷(TES,97%,Alfa Aeser),三异丙基硅烷(TiPS,99%,Alfa Aeser),甲基苯基硅烷(MPS,98%,Aldrich),二苯甲基硅烷(DPMS,97%,Alfa)、三乙氧基硅烷(TEOS,97%,Alfa Aeser),其它硅烷购自J&K Chemical。Tris(trimethylsilyl)silane (TTSS, 97%, Sigma-Aldrich), tris(triethylsilyl)silane (TTESS, 97%, Sigma-Aldrich), phenylsilane (PSH, 98%, Alfa Aeser), Diphenylsilane (DPS, 97%, Alfa Aeser), triphenylsilane (TPS, 99%, Alfa Aeser), diethylsilane (DES, 98%, Alfa Aeser), di-tert-butylsilane (DTBS, 95%, TCI), triethylsilane (TES, 97%, Alfa Aeser), triisopropylsilane (TiPS, 99%, Alfa Aeser), methylphenylsilane (MPS, 98%, Aldrich), II Benzylsilane (DPMS, 97%, Alfa), triethoxysilane (TEOS, 97%, Alfa Aeser), other silanes were purchased from J&K Chemical.
苯乙烯(St,99%)与丙烯酰胺(99%)购自Alfa Aeser。甲基丙烯酸甲酯(MMA)、丙烯酸甲酯(MA),丙烯酸丁酯(BA)、醋酸乙烯酯(VAc)、甲基丙烯酸三氟乙酯、甲基丙烯酸异冰片酯、4-乙烯基吡啶、N-乙烯基吡咯烷酮、异戊二烯等单体均为阿拉丁分析纯试剂,反应前用碱性Al 2O 3柱进行过柱处理。 Styrene (St, 99%) and acrylamide (99%) were purchased from Alfa Aeser. Methyl methacrylate (MMA), methyl acrylate (MA), butyl acrylate (BA), vinyl acetate (VAc), trifluoroethyl methacrylate, isobornyl methacrylate, 4-vinyl pyridine The monomers such as N-vinylpyrrolidone and isoprene are all Aladdin analytical reagents, and the column is treated with a basic Al 2 O 3 column before the reaction.
测试方法testing method
对四氢呋喃(THF)可溶的聚合物,其数均分子量(M n),重均分子量(M w)以及分子量分布多分散系数PDI(PDI=M w/M n)用马尔文Viscotek 270Max凝胶渗透色谱仪(GPC)系统进行测定。该系统配置有Viscotek VE1122溶剂传输单元,Viscotek VE 3580折光指数检测器,Viscotek 270激光光散射-差式粘度计双检测器,Viscotek VE2585柱温箱以及Viscotek T6000M GPC色谱柱。该系统按仪器厂商操作手册用聚苯乙烯标准聚合物PS 105k(Malvern,PolyCAL PS Std)进行校正,并进一步用聚苯乙烯标准聚合物PS 9290k(Polymer Standard Service USA,Inc)进行验证。数据采集分析软件:OmniSEC 5.02。测试条件:流动相,四氢呋喃;柱温,35℃;流动相流速:1.0mL/min。 For tetrahydrofuran (THF) soluble polymers, the number average molecular weight (M n ), weight average molecular weight (M w ) and molecular weight distribution polydispersity coefficient PDI (PDI = M w / M n ) with Malvern Viscotek 270Max gel The measurement was performed by a permeation chromatography (GPC) system. The system is equipped with Viscotek VE1122 solvent delivery unit, Viscotek VE 3580 refractive index detector, Viscotek 270 laser light scattering-differential viscometer dual detector, Viscotek VE2585 column oven and Viscotek T6000M GPC column. The system was calibrated with polystyrene standard polymer PS 105k (Malvern, PolyCAL PS Std) according to the instrument manufacturer's operating manual and further verified with polystyrene standard polymer PS 9290k (Polymer Standard Service USA, Inc). Data acquisition and analysis software: OmniSEC 5.02. Test conditions: mobile phase, tetrahydrofuran; column temperature, 35 ° C; mobile phase flow rate: 1.0 mL / min.
对THF不溶的聚乙烯基吡啶及聚乙烯基吡咯烷酮,其M n、M w以及PDI用岛津Prominence GPC分析系统进行测定。该系统配置有岛津RID-20A折光指数检测器,岛津SPD-15C紫外可见光检测器,岛津LC-16C溶剂传输单元,岛津CTO-16C柱温箱,以及Waters Styragel HR 5E DMF色谱柱。以一系列窄分散的PMMA标样(Polymer Laboratories)制作分子量校正曲线,数据采集分析软件:Labsolutions Essentia 5.82。测试条件:流动相,N,N-二甲基甲酰胺(含0.01M LiBr);柱温,50℃;流动相流速,0.3mL/min。聚丙烯酰胺分子量参照国家标准GB17514-2008用粘度法进行测定。聚丙烯酸的分子量参照文献(赵春凤,刘昆元,韩淑珍.北京化工大学学报,2002,29(1):51-55)用粘度法进行测定。 For THF-insoluble polyvinylpyridine and polyvinylpyrrolidone, M n , M w and PDI were measured using a Shimadzu Prominence GPC analysis system. The system is equipped with Shimadzu RID-20A refractive index detector, Shimadzu SPD-15C UV visible light detector, Shimadzu LC-16C solvent delivery unit, Shimadzu CTO-16C column oven, and Waters Styragel HR 5E DMF column. . Molecular weight calibration curves were prepared using a series of narrowly dispersed PMMA standards (Polymer Laboratories), data acquisition analysis software: Labsolutions Essentia 5.82. Test conditions: mobile phase, N,N-dimethylformamide (containing 0.01 M LiBr); column temperature, 50 ° C; mobile phase flow rate, 0.3 mL/min. The molecular weight of polyacrylamide was determined by the viscosity method in accordance with the national standard GB17514-2008. The molecular weight of polyacrylic acid is determined by the viscosity method by reference to Zhao Chunfeng, Liu Kunyuan, Han Shuzhen. Journal of Beijing University of Chemical Technology, 2002, 29(1): 51-55.
聚合物材料的核磁共振氢谱在Bruker Avance III 500MHz核磁共振波谱仪上测得。金属纳米粒子的粒径用FEI公司Tecnai G2F30高分辨透射电子显微镜(TEM)进行测定。正己烷溶液中金纳米粒子含量用PerkinElmer公司ELAN DRC-e电感耦合等离子体质谱仪(ICP-MS)测定。反应过程中单体的转化率用重量法测定。The nuclear magnetic resonance spectrum of the polymer material was measured on a Bruker Avance III 500 MHz NMR spectrometer. The particle diameter of the metal nanoparticles was measured by a FEI Tecnai G2F30 high resolution transmission electron microscope (TEM). The gold nanoparticle content in the n-hexane solution was measured by PerkinElmer ELAN DRC-e inductively coupled plasma mass spectrometer (ICP-MS). The conversion of the monomer during the reaction was determined gravimetrically.
实施例1Example 1
根据参考文献制备的金纳米粒子正己烷溶液用透射电子显微镜(TEM)测试,所得TEM图像和X射线能谱图(EDX)如图1所示,从图中可看出,金纳米粒子呈球形,分散性好,粒径大约在3~7nm之间,统计平均粒径为4.1nm。正己烷溶液中金含量用ICP-MS测得为0.75mg/mL。The gold nanoparticle n-hexane solution prepared according to the reference was tested by transmission electron microscopy (TEM). The obtained TEM image and X-ray energy spectrum (EDX) are shown in Fig. 1. As can be seen from the figure, the gold nanoparticles are spherical. It has good dispersibility, a particle size of about 3 to 7 nm, and a statistical average particle diameter of 4.1 nm. The gold content in the n-hexane solution was 0.75 mg/mL as measured by ICP-MS.
在离心管中加入上述100μL(3.81×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入2mL(0.019mol)MMA单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到70℃反应,在6min,50min,90min,130min,160min时用除氧的注射器与长针头从反应瓶中取样,用重量法测定各反应时间点单体的转化率,用GPC测定各点聚合物的重均分子量M n,重均分子量M w及PDI(PDI=M w/M n),绘制转化率-时间关系曲线、数均分子量-转化率曲线以及PDI-转化率关系曲线,结果如图2及图3所示。 Add 100 μL of the above-mentioned 100 μL (3.81×10 -7 mol Au) gold nanoparticle n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 2 mL (0.019 mol) of MMA monomer, shake for 30 s, and purge with nitrogen. Oxygen for 5 min, then the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, stirring was started, 10 μL (5.38×10 -5 mol) DPS was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 70 ° C. At 6 min, 50 min, 90 min, 130 min, and 160 min, an oxygen scavenging syringe and a long needle were used to sample from the reaction flask. The conversion rate of the monomer at each reaction time point was determined by gravimetric method, and the weight average of each point polymer was determined by GPC. molecular weight M n, weight average molecular weight M w and PDI (PDI = M w / M n), rendering the conversion - time curve, number average molecular weight - as well as the conversion curve PDI- conversion curve, results as shown in FIG. 2 and FIG. 3 is shown.
从图2中可看出,金纳米粒子催化MMA聚合反应的速率很块,随反应时间增加,单体转化率迅速增大,反应50min时转化率13.0%,160min时转化率达到71.1%。聚合物PMMA的数均分子量M n随转化率增加而线性地从1.6×10 5增加到5.0×10 5,聚合物的PDI保持在2.7以下(图3),使聚合反应呈现出活性聚合的特征,实验操作者从而可通过改变聚合反应的转化率,对聚合产物的分子量和分子量分布进行控制。 It can be seen from Fig. 2 that the rate of polymerization of MMA by gold nanoparticles is very high. As the reaction time increases, the monomer conversion rate increases rapidly. The conversion rate is 13.0% at 50 min and 71.1% at 160 min. PMMA polymer has a number average molecular weight M n linearly increased from 1.6 × 10 5 5.0 × 10 5, PDI of the polymer is maintained at 2.7 or less (FIG. 3) increasing with conversion, the polymerization reaction exhibit living polymerization wherein The experimental operator can thereby control the molecular weight and molecular weight distribution of the polymerization product by changing the conversion rate of the polymerization reaction.
实施例2Example 2
在Schlenk反应瓶中加入2.0mg(1.01×10 -5mol Au)有机溶剂可分散金纳米粉末,抽真空充氮气,用注射器加入2mL(0.019mol)预先充氮除氧的MMA单体,超声振荡1min,开启搅拌,随后用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到80℃反应4.5h后停止反应,取样测得单体的转化率85.2%,PMMA的重均分子量296万,数均分子量131万,PDI=2.25。 The 2.0 nm (1.01×10 -5 mol Au) organic solvent was added to the Schlenk reaction flask to disperse the gold nanopowder, vacuumed and filled with nitrogen, and 2 mL (0.019 mol) of pre-nitrogen-deoxygenated MMA monomer was added by syringe to ultrasonically oscillate. 1 min, stirring was started, then 10 μL (5.38×10 -5 mol) DPS was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 4.5 h. The reaction was stopped and the monomer conversion was 85.2%. PMMA The weight average molecular weight was 2.96 million, the number average molecular weight was 1.31 million, and PDI was 2.25.
实施例3Example 3
离心管中加入2mL(1.32×10 -6mol Au)金纳米粒子0.1mM PBS溶液,10000g离心20min,去掉上清夜,加入2mL四氢呋喃,超声振荡30s后10000g离心20min,去掉上清夜,再加入5mL(0.047mol)MMA单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到70℃反应10h后停止反应,取样测得单体的转化率59.0%,PMMA的重均分子量212万,数均分子量102万,PDI=2.07。 2 mL (1.32 × 10 -6 mol Au) gold nanoparticles 0.1 mM PBS solution was added to the centrifuge tube, centrifuged at 10,000 g for 20 min, the supernatant was removed, 2 mL of tetrahydrofuran was added, ultrasonically shaken for 30 s, centrifuged at 10000 g for 20 min, the supernatant was removed, and 5 mL was added ( 0.047mol) MMA monomer, ultrasonically shaken for 30s, degassed by nitrogen for 5min, then the monomer solution was added to the nitrogen and deoxidation Schlenk reaction bottle by syringe, and the mixture was stirred, and 10μL (8.10×10) was added with a micro syringe. -5 mol) PSH, stirred at room temperature for 5 min, then heated to 70 ° C for 10 h and then stopped. The conversion of the monomer was 59.0%, the weight average molecular weight of PMMA was 2.12 million, the number average molecular weight was 1.02 million, and PDI was 2.07.
实施例4Example 4
离心管中加入30μL(1.15×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入15mL(0.142mol)MMA单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入5μL(4.05×10 -5mol)PSH,室温下搅拌5min后升温到70℃反应22.5h后停止反应,取样测得单体的转化率83.1%,聚合物PMMA的重均分子量779万,数均分子量582万,PDI=1.34。 Add 30 μL (1.15×10 -7 mol Au) gold nanoparticles to n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 15 mL (0.142 mol) of MMA monomer, ultrasonically shake for 30 s, and deaerator with nitrogen for 5 min. Then, the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle by a syringe, and stirring was started. 5 μL (4.05×10 -5 mol) of PSH was added by a micro syringe, stirred at room temperature for 5 minutes, and then heated to 70 ° C for 22.5 hours. After the reaction was stopped, the conversion of the monomer was 83.1%, the weight average molecular weight of the polymer PMMA was 7.79 million, the number average molecular weight was 5.82 million, and the PDI was 1.34.
实施例5Example 5
离心管中加入100μL(3.81×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入10mL(0.094mol)MMA单体和10mL(0.094mol)甲苯溶剂,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到70℃反应11.5h后停止反应,取样测得单体的转化率35.0%,PMMA的重均分子量157万,数均分子量84万,PDI=1.87。 Add 100 μL (3.81×10 -7 mol Au) gold nanoparticles to n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 10 mL (0.094 mol) of MMA monomer and 10 mL (0.094 mol) of toluene solvent, and shake for 30 s. Nitrogen was bubbled and deaerated for 5 min. Then, the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, and stirring was started. 10 μL (5.38×10 -5 mol) of DPS was added using a micro syringe, and the mixture was stirred at room temperature for 5 min. After the temperature was raised to 70 ° C for 11.5 h, the reaction was stopped. The conversion of the monomer was 35.0%, the weight average molecular weight of PMMA was 1.57 million, the number average molecular weight was 840,000, and PDI was 1.87.
实施例6Example 6
离心管中加入1mL(3.81×10 -6mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入0.5mL(0.0047mol)MMA单体和9.5mL(0.090mol)甲苯溶剂,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入20μL(1.08×10 -4mol)DPS,室温下搅拌5min后升温到70℃反应17h后停止反应,取样测得单体的转化率62.9%,PMMA的重均分子量11万,数均分子量6.4万,PDI=1.72。 Add 1 mL (3.81×10 -6 mol Au) gold nanoparticle n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 0.5 mL (0.0047 mol) MMA monomer and 9.5 mL (0.090 mol) toluene solvent, and sonicate. After shaking for 30 s, deaerator with nitrogen for 5 min, then add the monomer solution to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, start stirring, add 20 μL (1.08×10 -4 mol) DPS with a micro syringe, at room temperature. After stirring for 5 min, the temperature was raised to 70 ° C for 17 h, and the reaction was stopped. The conversion of the monomer was 62.9%, the weight average molecular weight of PMMA was 110,000, the number average molecular weight was 64,000, and PDI was 1.72.
实施例7Example 7
将购买的Pd/C粉末催化剂用透射电子显微镜(TEM)测试,所得TEM图像和X射线能谱图(EDX)如图4所示,从图中可看出,Pd纳米粒子呈球形,均匀分散在活性炭粉末上,粒径在1-3nm之间,统计平均粒径为1.7nm。The purchased Pd/C powder catalyst was tested by transmission electron microscopy (TEM). The obtained TEM image and X-ray energy spectrum (EDX) are shown in Fig. 4. As can be seen from the figure, the Pd nanoparticles are spherical and uniformly dispersed. On the activated carbon powder, the particle diameter was between 1-3 nm, and the statistical average particle diameter was 1.7 nm.
在Schlenk反应瓶中加入20mg Pd/C(9.40×10 -6mol Pd),抽真空充氮气循环三次,用注射器加入2mL(0.019mol)预先除氧的MMA单体,超声振荡30s,开启搅拌,用微量注射 器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应16.5h后停止反应,取样测得单体的转化率53.0%,PMMA的重均分子量269万,数均分子量149万,PDI=1.81。 Add 20 mg Pd/C (9.40×10 -6 mol Pd) to the Schlenk reaction flask, vacuum-fill nitrogen three times, add 2 mL (0.019 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 30 s, and start stirring. 10 μL (8.10×10 -5 mol) PSH was added in a micro-syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 16.5 h. The reaction was stopped. The conversion of the monomer was 53.0%, and the weight average molecular weight of PMMA was 2.69 million. The number average molecular weight was 1.49 million, and PDI was 1.81.
实施例8Example 8
在Schlenk反应瓶中加入20mg Ru/C(9.90×10 -6mol Ru),抽真空充氮气循环三次,用注射器加入2mL(0.019mol)预先除氧的MMA单体,超声振荡30s,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应25h后停止反应,取样测得单体的转化率31.1%,PMMA的重均分子量449万,数均分子量191万,PDI=2.35。 Add 20 mg Ru/C (9.90×10 -6 mol Ru) to the Schlenk reaction flask, vacuum-fill nitrogen three times, add 2 mL (0.019 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 30 s, and start stirring. 10 μL (8.10×10 -5 mol) PSH was added in a micro-syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 25 h. The reaction was stopped. The conversion of the monomer was 31.1%, and the weight average molecular weight of PMMA was 4.49 million. The average molecular weight was 1.91 million, and PDI was 2.35.
实施例9Example 9
在Schlenk反应瓶中加入40mg Rh/C(1.94×10 -5mol Rh),抽真空充氮气循环三次,用注射器加入2mL(0.019mol)预先除氧的MMA单体,超声振荡30s,开启搅拌,用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到70℃反应24h后停止反应,取样测得单体的转化率47.4%,PMMA的重均分子量475万,数均分子量262万,PDI=1.81。 Add 40 mg of Rh/C (1.94×10 -5 mol Rh) to the Schlenk reaction flask, evacuate it under vacuum for three times, add 2 mL (0.019 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 30 s, and start stirring. 10 μL (5.38×10 -5 mol) of DPS was added in a micro-syringe, stirred at room temperature for 5 min, and then heated to 70 ° C for 24 h. The reaction was stopped. The conversion of the monomer was 47.4%, and the weight average molecular weight of PMMA was 4.75 million. The average molecular weight was 2.62 million, and PDI was 1.81.
实施例10Example 10
在Schlenk反应瓶中加入40mg Pt/C(1.03×10 -5mol Pt),抽真空充氮气循环三次,用注射器加入2mL(0.019mol)预先除氧的MMA单体,超声振荡30s,开启搅拌,用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到70℃反应13h后停止反应,取样测得单体的转化率24%,聚合物PMMA的重均分子量210万,数均分子量78万,PDI=2.69。 Add 40 mg of Pt/C (1.03×10 -5 mol Pt) to the Schlenk reaction flask, evacuate it under vacuum for three times, add 2 mL (0.019 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 30 s, and start stirring. 10 μL (5.38×10 -5 mol) of DPS was added in a micro-syringe, stirred at room temperature for 5 min, and then heated to 70 ° C for 13 h. The reaction was stopped. The conversion of the monomer was 24%, and the weight average molecular weight of the polymer PMMA was 2.1 million. , the number average molecular weight of 780,000, PDI = 2.69.
实施例11Example 11
在Schlenk反应瓶中加入20mg Ir/C(5.21×10 -6mol Ir),抽真空充氮气循环三次,用注射器加入2mL(0.019mol)预先除氧的MMA单体,超声振荡30s,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应34h后停止反应,取样测得单体的转化率25.6%,PMMA的重均分子量360万,数均分子量195万,PDI=1.85。 Add 20 mg Ir/C (5.21×10 -6 mol Ir) to the Schlenk reaction flask, vacuum-fill nitrogen three times, add 2 mL (0.019 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 30 s, and start stirring. 10 μL (8.10×10 -5 mol) PSH was added in a micro-syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 34 h. The reaction was stopped. The conversion of the monomer was 25.6%, and the weight average molecular weight of PMMA was 3.6 million. The average molecular weight was 1.95 million, and PDI was 1.85.
实施例12Example 12
在Schlenk反应瓶中加入10mg(1.79×10 -4mol)纳米铁粉,抽真空充氮气循环三次,用注射器加入5mL(0.047mol)预先除氧的MMA单体,超声振荡1min,剧烈搅拌下用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到70℃反应22.5h后停止反应,取样测得单体的转化率23.4%,PMMA的重均分子量280万,数均分子量171万,PDI=1.63。 Add 10 mg (1.79×10 -4 mol) of nano-iron powder to the Schlenk reaction flask, vacuum-fill nitrogen three times, add 5 mL (0.047 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 1 min, stir vigorously. 10μL (5.38×10 -5 mol) DPS was added to the micro-syringe, stirred at room temperature for 5 min, and then heated to 70 ° C for 22.5 h. The reaction was stopped. The conversion of the monomer was 23.4%, and the weight average molecular weight of PMMA was 2.8 million. The average molecular weight was 1.71 million and PDI=1.63.
实施例13Example 13
在Schlenk反应瓶中加入10mg(1.70×10 -4mol)纳米镍粉,抽真空充氮气循环三次,用注射器加入5mL(0.047mol)预先除氧的MMA单体,超声振荡1min,剧烈搅拌下用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到80℃反应30h后停止反应,取样测得单体的转化率25.2%,GPC测得PMMA的重均分子量197万,数均分子量92万,PDI=2.14。 Add 10 mg (1.70×10 -4 mol) of nano-nickel powder to the Schlenk reaction flask, vacuum-fill nitrogen three times, add 5 mL (0.047 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 1 min, stir vigorously. 10μL (5.38×10 -5 mol) DPS was added to the micro-syringe, stirred at room temperature for 5 min, then heated to 80 ° C for 30 h and then stopped. The sample was found to have a conversion of 25.2%. The weight average molecular weight of PMMA was 1.97 million. , the number average molecular weight of 920,000, PDI = 2.14.
实施例14Example 14
在Schlenk反应瓶中加入10mg(1.57×10 -4mol)纳米铜粉,抽真空充氮气循环三次,用注射器加入5mL(0.047mol)预先除氧的MMA单体,超声振荡1min,剧烈搅拌下用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应26h后停止 反应,取样测得单体的转化率26.7%,GPC测得PMMA的重均分子量301万,数均分子量161万,PDI=1.87。 Add 10mg (1.57×10 -4 mol) of nano copper powder to the Schlenk reaction bottle, vacuum and nitrogen three times, add 5mL (0.047mol) of pre-oxygenated MMA monomer with syringe, ultrasonically shake for 1min, use with vigorous stirring 10μL (8.10×10 -5 mol) PSH was added to the micro-syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 26 h. The reaction was stopped. The conversion of the monomer was 26.7%, and the weight average molecular weight of PMMA was 3.01 million. The number average molecular weight was 1.61 million, and PDI=1.87.
实施例15Example 15
在Schlenk反应瓶中加入15mg(1.39×10 -4mol)纳米银粉,抽真空充氮气循环三次,用注射器加入5mL(0.047mol)预先除氧的MMA单体,超声振荡1min,剧烈搅拌下用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应21h后停止反应,取样测得单体的转化率35.5%,GPC测得PMMA的重均分子量743万,数均分子量558万,PDI=1.33。 Add 15mg (1.39×10 -4 mol) of nano silver powder to the Schlenk reaction bottle, vacuum and nitrogen gas three times, add 5mL (0.047mol) pre-deoxygenated MMA monomer with syringe, ultrasonically shake for 1min, stir with trace 10 μL (8.10×10 -5 mol) PSH was added to the syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 21 h. The reaction was stopped. The conversion of the monomer was 35.5%, and the weight average molecular weight of PMMA was 7.43 million. The number average molecular weight was 5.58 million, and PDI=1.33.
实施例16Example 16
在Schlenk反应瓶中加入20mg(4.18×10 -4mol)纳米钛粉,抽真空充氮气循环三次,用注射器加入5mL(0.047mol)预先除氧的MMA单体,超声振荡1min,剧烈搅拌下用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到90℃反应30h后停止反应,取样测得单体的转化率32.2%,GPC测得PMMA的重均分子量227万,数均分子量127万,PDI=1.79。 Add 20 mg (4.18×10 -4 mol) of nano titanium powder to the Schlenk reaction flask, vacuum-fill nitrogen three times, add 5 mL (0.047 mol) of pre-deoxygenated MMA monomer with a syringe, shake it for 1 min, stir vigorously. 10μL (8.10×10 -5 mol) PSH was added to the micro-syringe, stirred at room temperature for 5 min, and then heated to 90 ° C for 30 h. The reaction was stopped. The conversion of the monomer was 32.2%, and the weight average molecular weight of PMMA was 2.27 million. , the number average molecular weight of 1.27 million, PDI = 1.79.
实施例17Example 17
在Schlenk反应瓶中加入25mg(1.36×10 -4mol)纳米钨粉,抽真空充氮气循环三次,用注射器加入5mL(0.047mol)预先除氧的MMA单体,超声振荡1min,剧烈搅拌下用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应24h后停止反应,取样测得单体的转化率28.8%,GPC测得PMMA的重均分子量207万,数均分子量83万,PDI=2.49。 Add 25mg (1.36×10 -4 mol) of nano-tungsten powder to Schlenk reaction flask, vacuum-fill nitrogen three times, add 5mL (0.047mol) pre-deoxygenated MMA monomer with syringe, ultrasonically shake for 1min, use with vigorous stirring 10μL (8.10×10 -5 mol) PSH was added to the micro-syringe, stirred at room temperature for 5 min, and then heated to 80 ° C for 24 h. The reaction was stopped. The conversion of the monomer was 28.8%, and the weight average molecular weight of PMMA was 2.07 million. , the number average molecular weight of 830,000, PDI = 2.49.
实施例18Example 18
在离心管中加入10mL(3.81×10 -5mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入1mL(0.0094mol)MMA单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入500μL(2.69×10 -3mol)DPS,室温下搅拌5min后升温到70℃反应12分钟后停止反应,取样测得单体的转化率5.0%。 Add 10 mL (3.81×10 -5 mol Au) gold nanoparticle n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 1 mL (0.0094 mol) of MMA monomer, shake for 30 s, and deaerate with nitrogen. 5 min, then the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, stirring was started, 500 μL (2.69×10 -3 mol) DPS was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 70 ° C. The reaction was stopped after a minute, and the conversion of the monomer was measured to be 5.0%.
将反应后的聚合物溶液用甲醇沉淀,所得PMMA用GPC测得的重均分子量3.2万,数均分子量1.7万,PDI=1.88。所得PMMA的核磁共振氢谱如图5所示。图中位于δ=7.2-7.8ppm之间的三组多重峰对应于引发剂DPS苯环上的质子,δ=3.6ppm的强峰对应于PMMA长链上甲氧基上的质子,根据二者的比例,计算得到PMMA聚合物的数均分子量为1.6万,与GPC测得的结果一致,表明每大分子链末端带有含硅的DPS引发剂基团。该官能团可进一步转化为其它功能基团而得到更有价值的功能高分子。The polymer solution after the reaction was precipitated with methanol, and the obtained PMMA had a weight average molecular weight of 32,000, a number average molecular weight of 17,000, and a PDI of 1.88 as measured by GPC. The nuclear magnetic resonance spectrum of the obtained PMMA is shown in Fig. 5. The three sets of multiple peaks between δ=7.2-7.8 ppm in the figure correspond to the protons on the benzene ring of the initiator DPS, and the strong peak of δ=3.6 ppm corresponds to the protons on the methoxy group of the long chain of PMMA, according to the two. The ratio of the PMMA polymer was calculated to be 16,000, which is consistent with the GPC measurement, indicating that a silicon-containing DPS initiator group is present at the end of each macromolecular chain. This functional group can be further converted into other functional groups to obtain a more valuable functional polymer.
实施例19Example 19
离心管中加入5mL(1.90×10 -5mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入1mL(0.0094mol)MMA单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入50μL(2.69×10 -4mol)DPS,将反应体系降温到0℃进行反应,24h后停止反应,取样测得单体的转化率51.1%,PMMA的重均分子量55万,数均分子量19万,PDI=2.89。 Add 5 mL (1.90×10 -5 mol Au) gold nanoparticle n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 1 mL (0.0094 mol) of MMA monomer, ultrasonically shake for 30 s, and deaerator with nitrogen for 5 min. Then, the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle by a syringe, and the stirring was started. 50 μL (2.69×10 -4 mol) of DPS was added by a micro syringe, and the reaction system was cooled to 0 ° C for reaction, after 24 hours. The reaction was stopped, and the conversion of the monomer was 51.1%, the weight average molecular weight of PMMA was 550,000, the number average molecular weight was 190,000, and PDI was 2.89.
实施例20Example 20
离心管中加入250μL(9.52×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入20mL(0.189mol)MMA单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(6.26×10 -5mol)TES,将反应体系降温到70℃进行反应,34h后停止反应,取样测得单体的转化率30.8%,PMMA的重均分子量636万,数均分子量448万,PDI=1.42。 250 μL (9.52×10 -7 mol Au) gold nanoparticles in n-hexane solution was added to the centrifuge tube, centrifuged at 16000 g for 30 min, the supernatant was removed, 20 mL (0.189 mol) of MMA monomer was added, ultrasonically shaken for 30 s, and oxygen was bubbled for 5 min. Then, the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle by a syringe, and the stirring was started. 10 μL (6.26×10 -5 mol) of TES was added by a micro syringe, and the reaction system was cooled to 70 ° C for reaction, after 34 hours. The reaction was stopped, and the conversion of the monomer was 30.8%, the weight average molecular weight of PMMA was 6.36 million, the number average molecular weight was 4.48 million, and PDI=1.42.
实施例21Example 21
离心管中加入200μL(7.62×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入10mL(0.108mol)醋酸乙烯酯单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的高压反应管(Ace pressure tubes,#15Ace-Thred),开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应72h后停止反应,取样测得单体的转化率54.9%,聚醋酸乙烯酯的重均分子量26万,数均分子量12万,PDI=2.17。 Add 200 μL (7.62×10 -7 mol Au) gold nanoparticles to n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 10 mL (0.108 mol) of vinyl acetate monomer, shake for 30 s, and purge with nitrogen. Oxygen for 5 min, then the monomer solution was added to a nitrogen-desulfurized high-pressure reaction tube (Ace pressure tubes, #15 Ace-Thred) by a syringe, and the stirring was started. 10 μL (8.10×10 -5 mol) PSH was added with a micro syringe, and the temperature was increased. After stirring for 5 min, the temperature was raised to 80 ° C for 72 h, and the reaction was stopped. The conversion of the monomer was 54.9%, the weight average molecular weight of polyvinyl acetate was 260,000, the number average molecular weight was 120,000, and the PDI was 2.17.
实施例22Example 22
离心管中加入0.5mL(1.90×10 -6mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入2mL(0.020mol)异戊二烯单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的高压反应管(Ace pressure tubes,#15Ace-Thred)中,开启搅拌,用微量注射器加入50μL(3.86×10 -4mol)DES,室温下搅拌5min后升温到130℃反应23h后停止反应,取样测得单体的转化率32.4%,聚异戊二烯的重均分子量9.0万,数均分子量4.5万,PDI=2.0。 Add 0.5 mL (1.90×10 -6 mol Au) gold nanoparticle n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 2 mL (0.020 mol) of isoprene monomer, ultrasonically shake for 30 s, and pass the nitrogen drum. The bubble was deaerated for 5 min, then the monomer solution was added to a nitrogen-desulfurized high-pressure reaction tube (Ace pressure tubes, #15 Ace-Thred) by a syringe, and the stirring was started, and 50 μL (3.86×10 -4 mol) was added using a micro syringe. DES, after stirring at room temperature for 5 min, the temperature was raised to 130 ° C for 23 h, and the reaction was stopped. The conversion of the monomer was 32.4%, the weight average molecular weight of polyisoprene was 90,000, the number average molecular weight was 45,000, and PDI was 2.0.
实施例23Example 23
离心管中加入100μL金纳米粒子正己烷溶液(3.81×10 -7mol Au),16000g离心30min,去掉上清夜,加入20mL丙烯酸丁酯单体(0.138mol),超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL DES(7.72×10 -5mol),室温下搅拌5min后升温到60℃反应16h后停止反应,取样测得单体的转化率54.4%,聚丙烯酸丁酯的重均分子量981万,数均分子量648万,PDI=1.51。 100 μL of gold nanoparticle n-hexane solution (3.81×10 -7 mol Au) was added to the centrifuge tube, centrifuged at 16000 g for 30 min, the supernatant was removed, 20 mL of butyl acrylate monomer (0.138 mol) was added, ultrasonically shaken for 30 s, and nitrogen gas was bubbled. Oxygen for 5 min, then the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, stirring was started, 10 μL of DES (7.72×10 -5 mol) was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 60 ° C. After 16 h, the reaction was stopped. The conversion of the monomer was 54.4%, the weight average molecular weight of polybutyl acrylate was 9.81 million, the number average molecular weight was 6.48 million, and PDI=1.51.
实施例24Example 24
离心管中加入20μL金纳米粒子正己烷溶液(7.61×10 -8mol Au),16000g离心30min,去掉上清夜,加入20mL丙烯酸甲酯单体(0.222mol),超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入6μL DES(4.63×10 -5mol),室温下搅拌5min后升温到50℃反应16h后停止反应,取样测得单体的转化率53.5%,聚丙烯酸甲酯的重均分子量827万,数均分子量611万,PDI=1.35。 Add 20 μL of gold nanoparticle n-hexane solution (7.61×10 -8 mol Au) to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 20 mL of methyl acrylate monomer (0.222 mol), ultrasonically shake for 30 s, and purge with nitrogen. Oxygen for 5 min, then the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, stirring was started, 6 μL of DES (4.63×10 -5 mol) was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 50 ° C. After 16 h, the reaction was stopped. The conversion of the monomer was 53.5%, the weight average molecular weight of polymethyl acrylate was 8.27 million, the number average molecular weight was 6.11 million, and PDI=1.35.
实施例25Example 25
离心管中加入1.0mL金纳米粒子正己烷溶液(3.81×10 -6mol Au),16000g离心30min,去掉上清夜,加入4mL(0.061mol)丙烯腈单体和1mL(0.013mol)N,N-二甲基甲酰胺溶剂,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到60℃反应30h后停止反应,测得单体的转化率18.0%,聚丙烯腈的重均分子量107万,数均分子量37万,PDI=2.89。 Add 1.0 mL of gold nanoparticle n-hexane solution (3.81×10 -6 mol Au) to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, and add 4 mL (0.061 mol) of acrylonitrile monomer and 1 mL (0.013 mol) of N, N- Dimethylformamide solvent, ultrasonic vibration for 30 s, bubbling oxygen for 5 min, then adding the monomer solution to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, stirring, and adding 10 μL (8.10×10) with a micro syringe. -5 mol) PSH, stirred at room temperature for 5 min, then heated to 60 ° C for 30 h and then stopped. The conversion of monomer was 18.0%, the weight average molecular weight of polyacrylonitrile was 1.07 million, and the number average molecular weight was 370,000. PDI=2.89 .
实施例26Example 26
在Schlenk反应瓶中加入1g(0.014mol)丙烯酰胺单体,抽真空充氮气,用注射器加入1.0mL(6.60×10 -7mol Au)金纳米粒子0.1mM PBS溶液,超声振荡30s,通氮气鼓泡除氧10min,开启搅拌,用微量注射器加入20μL(1.62×10 -4mol)PSH,室温下反应1.5h后停止反应,取样测得单体的转化率14.0%,粘度法测得聚丙烯酰胺的分子量为97万。 Add 1g (0.014mol) of acrylamide monomer to Schlenk reaction flask, vacuum-fill nitrogen, add 1.0mL (6.60×10 -7 mol Au) gold nanoparticles 0.1 mM PBS solution with syringe, ultrasonically shake for 30s, pass nitrogen drum The bubble was deoxidized for 10 min, the stirring was started, 20 μL (1.62×10 -4 mol) PSH was added with a micro syringe, and the reaction was stopped after 1.5 h at room temperature. The conversion of the monomer was determined by sampling, and the polyacrylamide was measured by the viscosity method. The molecular weight is 970,000.
实施例27Example 27
在Schlenk反应瓶中加入1.0mL(6.60×10 -7mol Au)金纳米粒子0.1mM PBS溶液,4g(0.056mol)丙烯酸单体和1mL(0.056mol)蒸馏水溶剂,超声振荡30s,通氮气鼓泡除氧10min,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌反应2h后停止反应,取样测得单体的转化率44.7%,粘度法测得聚丙烯酸的分子量为552万。 1.0 mL (6.60×10 -7 mol Au) gold nanoparticles 0.1 mM PBS solution, 4 g (0.056 mol) of acrylic acid monomer and 1 mL (0.056 mol) of distilled water solvent were added to the Schlenk reaction flask, and ultrasonically shaken for 30 s. After deaeration for 10 min, stir stirring, add 10 μL (8.10×10 -5 mol) PSH with a micro-syringe, stir the reaction at room temperature for 2 h, then stop the reaction. The sample was found to have a conversion of 44.7%. The viscosity of the polyacrylic acid was determined by viscosity method. It is 5.52 million.
实施例28Example 28
离心管中加入0.5mL(1.90×10 -6mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入2mL(0.017mol)苯乙烯单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应14h后停止反应,取样测得单体的转化率59.4%,聚苯乙烯的重均分子量75万,数均分子量26万,PDI=2.88 Add 0.5 mL (1.90×10 -6 mol Au) gold nanoparticle n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 2 mL (0.017 mol) of styrene monomer, ultrasonically shake for 30 s, and purge with nitrogen. Oxygen for 5 min, then the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, stirring was started, 10 μL (8.10×10 -5 mol) PSH was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 80 ° C. After 14h, the reaction was stopped. The conversion of the monomer was 59.4%, the weight average molecular weight of polystyrene was 750,000, and the number average molecular weight was 260,000. PDI=2.88
实施例29Example 29
离心管中加入50μL(1.90×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入2mL(0.035mol)甲基丙烯酸三氟乙酯单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(5.38×10 -5mol)DPS,室温下搅拌5min后升温到80℃反应11.5h后停止反应,取样测得单体的转化率85.1%,聚甲基丙烯酸三氟乙酯的重均分子量99万,数均分子量78万,PDI=1.27。 Add 50 μL (1.90×10 -7 mol Au) gold nanoparticles to n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 2 mL (0.035 mol) of trifluoroethyl methacrylate monomer, and shake for 30 s. Nitrogen was bubbled and deaerated for 5 min. Then, the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, and stirring was started. 10 μL (5.38×10 -5 mol) of DPS was added with a micro syringe, and the mixture was stirred at room temperature for 5 minutes. After the reaction was carried out at 80 ° C for 11.5 h, the reaction was stopped. The conversion of the monomer was 85.1%, the weight average molecular weight of the poly(trifluoroethyl methacrylate) was 990,000, the number average molecular weight was 780,000, and the PDI was 1.27.
实施例30Example 30
在Schlenk反应瓶中加入10.0mg(3.84×10 -5mol)TPS,抽真空充氮气。离心管中加入1.0mL金纳米粒子正己烷溶液(3.81×10 -6mol Au),16000g离心30min,去掉上清夜,加入10mL(0.044mol)甲基丙烯酸异冰片酯单体和3mL(0.035mol)二氧六环溶剂,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,室温下搅拌5min后升温到70℃反应6h后停止反应,取样测得单体的转化率52.7%,聚甲基丙烯酸异冰片酯的重均分子量628万,数均分子量441万,PDI=1.42。 10.0 mg (3.84 x 10 -5 mol) of TPS was added to the Schlenk reaction flask, and the mixture was evacuated under nitrogen. Add 1.0 mL of gold nanoparticle n-hexane solution (3.81×10 -6 mol Au) to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, and add 10 mL (0.044 mol) of isobornyl methacrylate monomer and 3 mL (0.035 mol). Dioxane solvent, ultrasonic vibration for 30s, bubbling oxygen for 5min, then adding the monomer solution to the nitrogen and deoxidation Schlenk reaction bottle with a syringe, stirring, stirring at room temperature for 5min, then heating to 70 °C reaction After 6 h, the reaction was stopped, and the conversion of the monomer was 52.7%. The weight average molecular weight of polyisobornyl methacrylate was 6.28 million, the number average molecular weight was 4.41 million, and PDI=1.42.
实施例31Example 31
离心管中加入100μL(3.81×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入5mL(0.047mol)N-乙烯基吡啶单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液加入到预先充氮除氧Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到80℃反应20.5h后停止反应,取样测得单体的转化率46.8%,聚(N-乙烯基吡啶)的重均分子量75.8万,数均分子量31.0万,PDI=2.45。 Add 100 μL (3.81×10 -7 mol Au) gold nanoparticles to n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 5 mL (0.047 mol) of N-vinylpyridine monomer, shake for 30 s, and pass the nitrogen drum. The bubble was deaerated for 5 min, then the monomer solution was added to a pre-nitrogen-deoxygenated Schlenk reaction bottle, and stirring was started. 10 μL (8.10×10 -5 mol) PSH was added with a micro syringe, stirred at room temperature for 5 min, and then heated to 80 ° C. After 20.5 h, the reaction was stopped. The conversion of the monomer was 46.8%, the weight average molecular weight of poly(N-vinylpyridine) was 758,000, the number average molecular weight was 311,000, and PDI was 2.45.
实施例32Example 32
离心管中加入0.5mL(3.30×10 -7mol Au)金纳米粒子0.1mM PBS溶液,10000g离心20min,去掉上清夜,加入2mL(0.019mol)N-乙烯基吡咯烷酮单体,超声振荡30s,通氮气鼓泡除氧5min,随后将单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌, 用微量注射器加入20μL(1.62×10 -4mol)PSH,室温下搅拌5min后升温到90℃反应18h后停止反应,取样测得单体的转化率43.2%,聚(N-乙烯基吡咯烷酮)的重均分子量47万,数均分子量18万,PDI=2.61。 Add 0.5 mL (3.30×10 -7 mol Au) gold nanoparticles 0.1 mM PBS solution to the centrifuge tube, centrifuge at 10,000 g for 20 min, remove the supernatant, add 2 mL (0.019 mol) N-vinylpyrrolidone monomer, and shake for 30 s. Nitrogen was bubbled and deaerated for 5 min. Then, the monomer solution was added to a nitrogen-desulfurized Schlenk reaction bottle with a syringe, and stirring was started. 20 μL (1.62×10 -4 mol) of PSH was added by a micro syringe, and the mixture was stirred at room temperature for 5 minutes. The reaction was stopped after reacting at 90 ° C for 18 h. The conversion of the monomer was 43.2%, the weight average molecular weight of poly(N-vinylpyrrolidone) was 470,000, the number average molecular weight was 180,000, and PDI was 2.61.
实施例33Example 33
离心管中加入200μL(7.62×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入10mL(0.094mol)MMA与10mL(0.069mol)丙烯酸丁酯混合单体,超声振荡30s,通氮气鼓泡除氧5min,随后将混合单体溶液加入到预先充氮除氧Schlenk反应瓶中,开启搅拌,用微量注射器加入20μL(1.08×10 -4mol)DPS,室温下搅拌5min后升温到70℃反应36h后停止反应,取样测得单体的转化率34.9%,共聚物的重均分子量370万,数均分子量261万,PDI=1.42。 Add 200 μL (7.62×10 -7 mol Au) gold nanoparticle n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, add 10 mL (0.094 mol) MMA and 10 mL (0.069 mol) butyl acrylate monomer, ultrasonic. After shaking for 30 s, deaerator with nitrogen for 5 min, then add the mixed monomer solution to the pre-nitrogen and deoxidation Schlenk reaction bottle, start stirring, add 20 μL (1.08×10 -4 mol) DPS with a micro syringe, stir at room temperature. After 5 minutes, the temperature was raised to 70 ° C for 36 h, and the reaction was stopped. The conversion of the monomer was 34.9%, the weight average molecular weight of the copolymer was 3.7 million, the number average molecular weight was 2.61 million, and PDI=1.42.
实施例34Example 34
离心管中加入50μL(1.90×10 -7mol Au)金纳米粒子正己烷溶液,16000g离心30min,去掉上清夜,加入2.3mL(0.022mol)MMA与2.3mL(0.022mol)N-乙烯基吡啶混合单体,超声振荡30s,通氮气鼓泡除氧5min,随后将混合单体溶液用注射器加入到充氮除氧的Schlenk反应瓶中,开启搅拌,用微量注射器加入10μL(8.10×10 -5mol)PSH,室温下搅拌5min后升温到70℃反应39.5h后停止反应,取样测得单体的转化率56.8%,共聚物的重均分子量45万,数均分子量15.4万,PDI=2.92。 Add 50 μL (1.90×10 -7 mol Au) gold nanoparticles to n-hexane solution to the centrifuge tube, centrifuge at 16000 g for 30 min, remove the supernatant, and add 2.3 mL (0.022 mol) of MMA and 2.3 mL (0.022 mol) of N-vinylpyridine. The monomer was ultrasonically shaken for 30 s, and degassed by nitrogen for 5 min. Then, the mixed monomer solution was added into a nitrogen-desulfurized Schlenk reaction bottle with a syringe, and the mixture was stirred, and 10 μL (8.10×10 -5 mol) was added using a micro syringe. PSH was stirred at room temperature for 5 min, then heated to 70 ° C for 39.5 h, and the reaction was stopped. The conversion of the monomer was 56.8%, the weight average molecular weight of the copolymer was 450,000, the number average molecular weight was 154,000, and PDI was 2.92.
对比例1Comparative example 1
根据文献(何姣,郭文迅,彭荡,等.应用化工,2011,40(2):210-214),一个典型的自由基聚合例子如下:According to the literature (He Wei, Guo Wenxun, Peng Dang, et al. Applied Chemicals, 2011, 40(2): 210-214), a typical example of free radical polymerization is as follows:
单体:甲基丙烯酸甲酯:甲基丙烯酸:丙烯酸丁酯=50:25:25;Monomer: methyl methacrylate: methacrylic acid: butyl acrylate = 50:25:25;
引发剂:偶氮二异丁腈、偶氮二异戊腈、偶氮二异庚腈,用量0.6-2.0wt%;Initiator: azobisisobutyronitrile, azobisisovaleronitrile, azobisisoheptanenitrile, the amount of 0.6-2.0 wt%;
反应温度:70-85℃;Reaction temperature: 70-85 ° C;
聚合物数均分子量:2772-14656;分子量分布多分散指数:3.66-17.42。Polymer number average molecular weight: 2772-14656; molecular weight distribution polydispersity index: 3.66-174.42.
与本发明的方法相比,传统自由基聚合的引发剂使用量较大,所得聚合物分子量低,分子量分布多分散系数很大。Compared with the method of the present invention, the conventional radical polymerization initiator is used in a large amount, the obtained polymer has a low molecular weight, and the molecular weight distribution has a large polydispersity coefficient.
对比例2Comparative example 2
根据文献(颜德岳,吴邦媛,裘祖文,等.同济大学学报,1980,4:34-43),一个典型的阴离子聚合例子如下:According to the literature (Yan Deyue, Wu Bangyuan, Qi Zuwen, et al. Journal of Tongji University, 1980, 4: 34-43), a typical example of anionic polymerization is as follows:
单体:甲基丙烯酸甲酯,浓度1.23mol/L;Monomer: methyl methacrylate, concentration 1.23mol / L;
溶剂:甲苯;Solvent: toluene;
引发剂:正丁基锂,浓度:2.55×10 -2mol/L; Initiator: n-butyl lithium, concentration: 2.55 × 10 -2 mol / L;
反应温度:-40℃;封管中反应,反应时间:90分钟;Reaction temperature: -40 ° C; reaction in a sealed tube, reaction time: 90 minutes;
分子量(以聚合物特性粘数表示):[η]=164.1ml/g;分子量分布很宽,呈现双峰分布。Molecular weight (expressed as the intrinsic viscosity of the polymer): [η] = 164.1 ml/g; the molecular weight distribution is broad and exhibits a bimodal distribution.
与本发明的方法相比,甲基丙烯酸甲酯的阴离子聚合反应条件苛刻,正丁基锂极活泼,需在完全无水条件下封管中低温条件下进行反应,所得聚合物分子量分布很宽,呈现双峰分布。Compared with the method of the present invention, the anionic polymerization reaction condition of methyl methacrylate is severe, n-butyl lithium is extremely active, and it is required to carry out the reaction under low temperature conditions under a completely anhydrous condition, and the obtained polymer has a wide molecular weight distribution. , showing a bimodal distribution.
对比例3Comparative example 3
根据文献(Hitoshi Abe,Kiyokazu Imai,Masakazu Matsumoto.Journal of Polymer Science  Part B:Polymer Letters,1965,3,1053-1058),一个典型的配位聚合例子如下:According to the literature (Hitoshi Abe, Kiyokazu Imai, Masakazu Matsumoto. Journal of Polymer Science Part B: Polymer Letters, 1965, 3, 1053-1058), a typical example of coordination polymerization is as follows:
单体:甲基丙烯酸甲酯,浓度10vol%;Monomer: methyl methacrylate, concentration 10vol%;
溶剂:甲苯;Solvent: toluene;
催化剂:齐格-纳塔催化剂TiCl 4+AlEt 3Catalyst: Zieg-Natta catalyst TiCl 4 + AlEt 3 ;
反应温度:-78℃;反应时间:18h;Reaction temperature: -78 ° C; reaction time: 18 h;
转化率:88.5%;分子量:25.5万。Conversion rate: 88.5%; molecular weight: 255,000.
与本发明的方法相比,甲基丙烯酸甲酯的配位聚合反应条件苛刻,TiCl 4与AlEt 3极活泼,需在完全无水条件下温度极低的环境中进行反应,所得聚合物分子量较低。 Compared with the method of the present invention, the coordination polymerization conditions of methyl methacrylate are severe, and TiCl 4 and AlEt 3 are extremely active, and it is required to carry out the reaction in an extremely low temperature environment under completely anhydrous conditions, and the molecular weight of the obtained polymer is relatively high. low.

Claims (10)

  1. 一种过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述的方法为:A method for catalyzing a polymerization of a vinyl monomer by a transition metal nanoparticle, characterized in that the method is:
    在惰性气体保护下,将单体、催化剂、引发剂、溶剂混合均匀,于0~130℃下反应0.2~72h,之后反应体系经后处理,即得产品;Under the protection of inert gas, the monomer, catalyst, initiator and solvent are uniformly mixed and reacted at 0-130 ° C for 0.2-72 h, after which the reaction system is post-treated to obtain a product;
    所述单体为乙烯基不饱和单体;所述催化剂为过渡金属纳米颗粒;所述引发剂为有机硅氢化合物;The monomer is an ethylenically unsaturated monomer; the catalyst is a transition metal nanoparticle; the initiator is an organosilicon hydrogen compound;
    所述单体、引发剂、催化剂、溶剂的投料物质的量之比为1.0:0.0002~0.3:0.0000003~0.01:0~20。The ratio of the amount of the monomer, the initiator, the catalyst, and the solvent to be charged is 1.0:0.0002 to 0.3:0.0000003 to 0.01:0 to 20.
  2. 如权利要求1所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述单体、引发剂、催化剂、溶剂的投料物质的量之比为1:0.001~0.1:0.000001~0.001:0~1。The method of claim 1, wherein the ratio of the amount of the monomer, the initiator, the catalyst, and the solvent to be charged is 1:0.001 to 0.1: 0.000001 to 0.001: 0 to 1.
  3. 如权利要求1所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述反应的温度为50~100℃。A method of catalyzing a polymerization of a vinyl monomer by transition metal nanoparticles according to claim 1, wherein the temperature of the reaction is from 50 to 100 °C.
  4. 如权利要求1所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述反应的时间为1~36h。The method of claim 1, wherein the reaction is carried out for a period of from 1 to 36 hours.
  5. 如权利要求1所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述单体为下列单体中的一种,或者两种以上互溶单体的任意比例混合物:A method of catalyzing a polymerization of a vinyl monomer by transition metal nanoparticles according to claim 1, wherein the monomer is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
    苯乙烯、对氯甲基苯乙烯、α-甲基苯乙烯、对氟苯乙烯、对氯苯乙烯、对溴苯乙烯、对三氟甲基苯乙烯、对二乙烯基苯、甲基丙烯酸甲酯、甲基丙烯酸乙酯、甲基丙烯酸丙酯、甲基丙烯酸异丙酯、甲基丙烯酸丁酯、甲基丙烯酸异丁酯、甲基丙烯酸辛酯、甲基丙烯酸异辛酯、甲基丙烯酸月桂酯、甲基丙烯酸苯酯、甲基丙烯酸缩水甘油醚酯、二缩三乙二醇甲基丙烯酸酯、甲基丙烯酸2-乙基已酯、甲基丙烯酸异冰片酯、甲基丙烯酸羟乙酯、甲基丙烯酸羟丙酯、甲基丙烯酸羟丁酯、甲基丙烯酸三氟乙酯、甲基丙烯酸六氟丁酯、N,N-二甲胺基乙基甲基丙烯酸酯、N,N-二乙胺基乙基甲基丙烯酸酯、二甲基丙烯酸1,4-丁二醇酯、丙烯酸甲酯、丙烯酸乙酯、丙烯酸丙酯、丙烯酸异丙酯、丙烯酸丁酯、丙烯酸异丁酯、丙烯酸辛酯、丙烯酸异辛酯、丙烯酸月桂酯、丙烯酸羟乙酯、丙烯酸羟丙酯及、丙烯酸羟丁酯、N,N-二甲胺基乙基丙烯酸酯、N,N-二乙胺基乙基丙烯酸酯、丙烯酸三氟乙酯、丙烯酸缩水甘油醚酯、二缩三乙二醇丙烯酸酯、丙烯酸六氟丁酯、丙烯酸2-乙基己酯、丙烯酸苯酯、二丙烯酸1,4-丁二醇酯、丙烯酸异冰片酯、丙烯酰胺、甲基丙烯酰胺、N-异丙基丙烯酰胺、N-羟甲基丙烯酰胺、N-(2-羟丙基)甲基丙烯酰胺、N-甲基丙烯酰胺、N,N-二甲基丙烯酰胺、N-特丁基丙烯酰胺、N-正丁基丙烯酰胺、亚甲基双丙烯酰胺、醋酸乙烯酯、氯乙酸乙烯酯、丙酸乙烯酯、丁酸乙烯酯、丙烯腈、甲基丙烯腈、丙烯酸、甲基丙烯酸、4-乙烯基吡啶、N-乙烯基吡咯烷酮、氯乙烯、异戊二烯或丁二烯。Styrene, p-chloromethylstyrene, α-methylstyrene, p-fluorostyrene, p-chlorostyrene, p-bromostyrene, p-trifluoromethylstyrene, p-divinylbenzene, methacrylic acid Ester, ethyl methacrylate, propyl methacrylate, isopropyl methacrylate, butyl methacrylate, isobutyl methacrylate, octyl methacrylate, isooctyl methacrylate, methacrylic acid Lauryl ester, phenyl methacrylate, glycidyl methacrylate, triethylene glycol methacrylate, 2-ethylhexyl methacrylate, isobornyl methacrylate, hydroxyethyl methacrylate Ester, hydroxypropyl methacrylate, hydroxybutyl methacrylate, trifluoroethyl methacrylate, hexafluorobutyl methacrylate, N,N-dimethylaminoethyl methacrylate, N, N -diethylaminoethyl methacrylate, 1,4-butylene glycol dimethacrylate, methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate, isobutyl acrylate , octyl acrylate, isooctyl acrylate, lauryl acrylate, hydroxy acrylate Ester, hydroxypropyl acrylate and hydroxybutyl acrylate, N,N-dimethylaminoethyl acrylate, N,N-diethylaminoethyl acrylate, trifluoroethyl acrylate, glycidyl acrylate , Triethylene glycol acrylate, hexafluorobutyl acrylate, 2-ethylhexyl acrylate, phenyl acrylate, 1,4-butylene glycol diacrylate, isobornyl acrylate, acrylamide, methacryl Amide, N-isopropylacrylamide, N-methylol acrylamide, N-(2-hydroxypropyl)methacrylamide, N-methyl acrylamide, N,N-dimethyl acrylamide, N -tert-butyl acrylamide, N-n-butyl acrylamide, methylene bis acrylamide, vinyl acetate, vinyl chloroacetate, vinyl propionate, vinyl butyrate, acrylonitrile, methacrylonitrile, acrylic acid , methacrylic acid, 4-vinyl pyridine, N-vinyl pyrrolidone, vinyl chloride, isoprene or butadiene.
  6. 如权利要求5所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述单体为下列单体中的一种,或者两种以上互溶单体的任意比例混合物:A method of catalyzing a polymerization of a vinyl monomer by a transition metal nanoparticle according to claim 5, wherein the monomer is one of the following monomers, or a mixture of two or more miscible monomers in any ratio:
    苯乙烯、对氯甲基苯乙烯、对氯苯乙烯、甲基丙烯酸甲酯、甲基丙烯酸丁酯、甲基丙烯酸月桂酯、甲基丙烯酸2-乙基已酯、甲基丙烯酸缩水甘油醚酯、甲基丙烯酸异冰片酯、甲基丙烯酸三氟乙酯、甲基丙烯酸六氟丁酯、丙烯酸甲酯、丙烯酸乙酯、丙烯酸丁酯、丙烯酸月桂酯、丙烯酸羟乙酯、丙烯酸缩水甘油醚酯、丙烯酸六氟丁酯、丙烯酰胺、甲基丙烯酰胺、N-异丙基丙烯酰胺、N-羟甲基丙烯酰胺、N,N-二甲基丙烯酰胺、亚甲基双丙烯酰胺、醋酸乙烯酯、氯乙酸乙烯酯、丙酸乙烯酯、丙烯腈、丙烯酸、4-乙烯基吡啶、N-乙烯基吡咯烷酮、氯乙 烯或异戊二烯。Styrene, p-chloromethylstyrene, p-chlorostyrene, methyl methacrylate, butyl methacrylate, lauryl methacrylate, 2-ethylhexyl methacrylate, glycidyl methacrylate , isobornyl methacrylate, trifluoroethyl methacrylate, hexafluorobutyl methacrylate, methyl acrylate, ethyl acrylate, butyl acrylate, lauryl acrylate, hydroxyethyl acrylate, glycidyl acrylate , hexafluorobutyl acrylate, acrylamide, methacrylamide, N-isopropyl acrylamide, N-methylol acrylamide, N,N-dimethyl acrylamide, methylene bis acrylamide, vinyl acetate Ester, vinyl chloroacetate, vinyl propionate, acrylonitrile, acrylic acid, 4-vinyl pyridine, N-vinyl pyrrolidone, vinyl chloride or isoprene.
  7. 如权利要求1所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述催化剂为下列过渡金属纳米颗粒中的一种或两种以上任意比例的混合物:The method of claim 1, wherein the catalyst is one or a mixture of two or more of the following transition metal nanoparticles:
    金纳米颗粒、银纳米颗粒、铜纳米颗粒、铂纳米颗粒、钯纳米颗粒、镍纳米颗粒、铑纳米颗粒、铼纳米颗粒、钌纳米颗粒、铁纳米颗粒、钴纳米颗粒、铱纳米颗粒、钨纳米颗粒、钛纳米颗粒、钒纳米颗粒、锰纳米颗粒、钼纳米颗粒或铬纳米颗粒。Gold nanoparticles, silver nanoparticles, copper nanoparticles, platinum nanoparticles, palladium nanoparticles, nickel nanoparticles, ruthenium nanoparticles, ruthenium nanoparticles, ruthenium nanoparticles, iron nanoparticles, cobalt nanoparticles, ruthenium nanoparticles, tungsten nanoparticles Particles, titanium nanoparticles, vanadium nanoparticles, manganese nanoparticles, molybdenum nanoparticles or chromium nanoparticles.
  8. 如权利要求7所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述过渡金属纳米颗粒的平均粒径在1~100nm之间;所述过渡金属纳米颗粒的存在形式为固体粉末、纳米颗粒溶液或纳米颗粒负载到固体基质表面的形式。The method of claim 7, wherein the transition metal nanoparticles have an average particle diameter of between 1 and 100 nm; and the transition metal nanoparticles are present. The form is a solid powder, a nanoparticle solution or a form of nanoparticles loaded onto the surface of a solid substrate.
  9. 如权利要求1所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述引发剂为下列有机硅氢化合物中的一种或两种以上任意比例的混合物:The method of claim 1, wherein the initiator is one or a mixture of two or more of the following organosilicon compounds:
    苯硅烷、正丁基硅烷、正己基硅烷、环己基硅烷、正十八烷基硅烷、二苯基硅烷、二丙基硅烷、二异丙基硅烷、二正丁基硅烷、二异丁基硅烷、二叔丁基硅烷、二正己基硅烷、二环己基硅烷、甲基苯基硅烷、苯基氯硅烷、三苯基硅烷、三乙基硅烷、三丙基硅烷、三异丙基硅烷、三正丁基硅烷、三异丁基硅烷、三叔丁基硅烷、三正己基硅烷、三环己基硅烷、三正辛基硅烷、正丁基二甲基硅烷、异丁基二甲基硅烷、叔丁基二甲基硅烷、三(三甲基硅基)硅烷、三(三乙基硅基)硅烷、三氯硅烷、甲基二氯硅烷、乙基二氯硅烷、苯基二氯硅烷、二甲基氯硅烷、二苯基氯硅烷、二异丙基氯硅烷、二叔丁基氯硅烷、甲基苯基氯硅烷、二甲基烯丙基硅烷、甲基二苯基硅烷、二甲基苯基硅烷、二甲基正己基硅烷、二甲基正丁基硅烷、正十八烷基二乙氧基硅烷、三甲氧基硅烷、三乙氧基硅烷、三丙氧基硅烷、三异丙氧基硅烷、三丁氧基硅烷、三叔丁氧基硅烷、甲基二甲氧基硅烷、甲基二乙氧基硅烷、苯基二甲氧基硅烷或苯基二乙氧基硅烷。Benzylsilane, n-butylsilane, n-hexylsilane, cyclohexylsilane, n-octadecylsilane, diphenylsilane, dipropylsilane, diisopropylsilane, di-n-butylsilane, diisobutylsilane , di-tert-butylsilane, di-n-hexylsilane, dicyclohexylsilane, methylphenylsilane, phenylchlorosilane, triphenylsilane, triethylsilane, tripropylsilane, triisopropylsilane, three n-Butylsilane, triisobutylsilane, tri-tert-butylsilane, tri-n-hexylsilane, tricyclohexylsilane, tri-n-octylsilane, n-butyldimethylsilane, isobutyldimethylsilane, uncle Butyldimethylsilane, tris(trimethylsilyl)silane, tris(triethylsilyl)silane, trichlorosilane, methyldichlorosilane, ethyldichlorosilane, phenyldichlorosilane, two Methylchlorosilane, diphenylchlorosilane, diisopropylchlorosilane, di-tert-butylchlorosilane, methylphenylchlorosilane, dimethylallylsilane, methyldiphenylsilane, dimethyl Phenylsilane, dimethyl-n-hexylsilane, dimethyl-n-butylsilane, n-octadecyldiethoxysilane, trimethoxy Silane, triethoxysilane, tripropoxysilane, triisopropoxysilane, tributoxysilane, tri-tert-butoxysilane, methyldimethoxysilane, methyldiethoxysilane, Phenyldimethoxysilane or phenyldiethoxysilane.
  10. 如权利要求1所述的过渡金属纳米颗粒催化乙烯基单体聚合反应的方法,其特征在于,所述溶剂为下列溶剂中的一种或两种以上互溶溶剂的任意比例混合物:The method for catalyzing the polymerization of a vinyl monomer by the transition metal nanoparticles according to claim 1, wherein the solvent is one or a mixture of two or more miscible solvents in any ratio of the following solvents:
    正己烷、环己烷、石油醚、庚烷、辛烷、苯、甲苯、对二甲苯、十氢萘、二氯甲烷、三氯甲烷、四氯化碳、三氯乙烯、四氯乙烯、乙醚、正丁醚、乙二醇二甲醚、二乙二醇二甲醚、三乙二醇二甲醚、四氢呋喃、二氧六环、二苯醚、丙酮、乙酰丙酮、丁酮、环己酮、乙酸乙酯、乙酸丙酯、乙酸丁酯、甲醇、乙醇、异丙醇、正丁醇、异丁醇、环己醇、乙二醇、一缩二乙二醇、二缩三乙二醇、水、N,N-二甲基甲酰胺、N-甲基甲酰胺、N-甲基乙酰胺、二甲基亚砜、环丁砜、N-甲基吡咯烷酮或γ-丁内酯。Hexane, cyclohexane, petroleum ether, heptane, octane, benzene, toluene, p-xylene, decahydronaphthalene, dichloromethane, chloroform, carbon tetrachloride, trichloroethylene, tetrachloroethylene, diethyl ether , n-butyl ether, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, triethylene glycol dimethyl ether, tetrahydrofuran, dioxane, diphenyl ether, acetone, acetylacetone, methyl ethyl ketone, cyclohexanone , ethyl acetate, propyl acetate, butyl acetate, methanol, ethanol, isopropanol, n-butanol, isobutanol, cyclohexanol, ethylene glycol, diethylene glycol, triethylene glycol , water, N,N-dimethylformamide, N-methylformamide, N-methylacetamide, dimethyl sulfoxide, sulfolane, N-methylpyrrolidone or γ-butyrolactone.
PCT/CN2017/116807 2017-02-09 2017-12-18 Method for catalyzing polymerization of vinyl monomers by means of transition metal nanoparticle WO2018145517A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201710070848.5A CN108409894B (en) 2017-02-09 2017-02-09 Method for catalyzing vinyl monomer polymerization reaction by transition metal nanoparticles
CN201710070848.5 2017-02-09

Publications (1)

Publication Number Publication Date
WO2018145517A1 true WO2018145517A1 (en) 2018-08-16

Family

ID=63107900

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2017/116807 WO2018145517A1 (en) 2017-02-09 2017-12-18 Method for catalyzing polymerization of vinyl monomers by means of transition metal nanoparticle

Country Status (2)

Country Link
CN (1) CN108409894B (en)
WO (1) WO2018145517A1 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114588953B (en) * 2022-04-01 2023-12-01 丹东明珠特种树脂有限公司 Methanol extraction deacidification agent for etherification preparation process and preparation method thereof
CN114773660B (en) * 2022-04-26 2023-08-29 浙江工业大学 Porous ultrahigh molecular weight fluorine-containing olefin hollow microsphere and preparation method thereof
CN115181465A (en) * 2022-07-07 2022-10-14 浙江工业大学 Preparation method of molecularly imprinted polymer coating capable of specifically recognizing enrofloxacin based on silver nanoparticles
CN115746185B (en) * 2022-12-13 2024-04-26 丽水学院 Preparation method of polymethyl methacrylate with ultrahigh molecular weight

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102039199A (en) * 2009-10-16 2011-05-04 中国科学院化学研究所 Clay catalyst carrier and preparation method and application thereof

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2625027A1 (en) * 1976-06-03 1977-12-15 Bayer Ag Free radical catalysts, esp. for unsatd. polyesters - are prepd. by reacting a metal alkyl or aryl, a diaryl ketone and water, an acid halide, an anhydride or a silane
JPS55129441A (en) * 1979-03-28 1980-10-07 Furukawa Electric Co Ltd:The Method of crosslinking poly-alpha-olefin resin
US4866145A (en) * 1988-04-01 1989-09-12 E. I. Du Pont De Nemours And Company Catalyst for group transfer polymerization
JP4814422B2 (en) * 2000-11-09 2011-11-16 株式会社カネカ Method for producing polymer and polymer
WO2008063680A2 (en) * 2006-01-27 2008-05-29 Nano Dynamics Life Sciences, Inc. Treated articles and methods of treating articles
JP2008063360A (en) * 2006-09-04 2008-03-21 Kyoto Univ Polyphenylacetylenic polymer, method for producing the same and phenylacetylene derivative
WO2009056401A1 (en) * 2007-09-27 2009-05-07 Basf Se Isolable and redispersable transition metal nanoparticles their preparation and use as ir absorbers
KR101070542B1 (en) * 2007-11-28 2011-10-05 주식회사 엘지화학 Catalytic composition for producing 1-alkene and acrylates copolymer and method for producing 1-alkene and acrylates copolymer
JP2010168545A (en) * 2008-12-25 2010-08-05 Sumitomo Chemical Co Ltd CATALYST FOR POLYMERIZATION OF alpha-OLEFIN AND MANUFACTURING METHOD FOR alpha-OLEFIN POLYMER
CN102731693B (en) * 2011-04-15 2014-09-24 中国科学院化学研究所 Polyolefin catalyst adopting carbon nanotubes as carriers and preparation method thereof
US8541520B1 (en) * 2013-01-21 2013-09-24 King Fahd University Of Petroleum And Minerals Method of making high-density polyethylene with titania-iron nanofillers
CN104031181A (en) * 2014-06-10 2014-09-10 浙江工业大学 Catalytic system for atom transfer radical polymerization reaction and application thereof

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102039199A (en) * 2009-10-16 2011-05-04 中国科学院化学研究所 Clay catalyst carrier and preparation method and application thereof

Also Published As

Publication number Publication date
CN108409894B (en) 2020-12-25
CN108409894A (en) 2018-08-17

Similar Documents

Publication Publication Date Title
WO2018145517A1 (en) Method for catalyzing polymerization of vinyl monomers by means of transition metal nanoparticle
US7825199B1 (en) Catalytic processes for the controlled polymerization of free radically (co)polymerizable monomers and functional polymeric systems prepared thereby
KR101712233B1 (en) Binder composition for all-solid-state battery and slurry for all-solid-state battery electrode
JP5419081B2 (en) Thermoplastic composite material
Liu et al. Water-dispersible carbon black nanocomposites prepared by surface-initiated atom transfer radical polymerization in protic media
Chen et al. Synthesis and characterization of poly (N-isopropylacrylamide)-coated polystyrene microspheres with silver nanoparticles on their surfaces
US9598553B2 (en) Metal nanoparticle composite and method for producing the same
JP6215403B2 (en) Organic-inorganic composite particles, dispersion containing the same, and resin composition
CN114377727B (en) Embedding type metal catalyst
Sakellariou et al. Enhanced polymer grafting from multiwalled carbon nanotubes through living anionic surface-initiated polymerization
Riazi et al. In situ synthesis of silica/polyacrylate nanocomposite particles simultaneously bearing carboxylate and sulfonate functionalities via soap-free seeded emulsion polymerization
WO2009139450A1 (en) Alumina composite material
Chen et al. Controllable preparation of polymer brushes from mesoporous silica SBA-15 via surface-initiated ARGET ATRP
Priftis et al. Polymer grafted Janus multi-walled carbon nanotubes
TWI428357B (en) Conjugated diene-vinyl aromatic hydrocarbon copolymer and manufacturing method of the same
Agudelo et al. A novel method for the synthesis of polystyrene-graft-silica particles using random copolymers based on styrene and triethoxyvinylsilane
Peng et al. A simple polymerizable polysoap greatly enhances the grafting efficiency of the “grafting-to” functionalization of multiwalled carbon nanotubes
EP1637550B1 (en) Catalytic processes for the controlled polymerization of free radically (co) polymerizable monomers and functional polymeric systems prepared thereby
Qian et al. A new ferrocene/disulfide-containing methacrylate monomer: synthesis, ATRP and nanocomposite
TW201226425A (en) Conjugated diene-vinyl aromatic hydrocarbon copolymer and manufacturing method of the same
Lu et al. Controllable synthesis of nanosilica surface-grafted PMMA macromonomers via catalytic chain transfer polymerization
Jaisankar et al. Single-electron transfer living radical copolymerization of SWCNT-g-PMMA via graft from approach
CN107442168B (en) Double-component hybrid particle-loaded catalyst and preparation method thereof
Yao et al. Direct grafting poly (methyl methacrylate) from TiO2 nanoparticles via Cu2+‐amine redox‐initiated radical polymerization: An advantage of monocenter initiation
Pietrasik et al. Macromolecular Templates for Synthesis of Inorganic Nanoparticles

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 17895863

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 17895863

Country of ref document: EP

Kind code of ref document: A1