End group functionalized liquid butadiene polymer, preparation method and application thereof, composition and application thereof, and polymer coating

Abstract

The invention relates to the field of polymers, and discloses an end group functionalized liquid butadiene polymer and a preparation method and application thereof, a composition containing the end group functionalized liquid butadiene polymer and application thereof, and a polymer coating. The end-capping efficiency of the end group functionalized liquid butadiene polymer is 0.8 to 1; on the basis of the total weight of the liquid butadiene polymer, the content of the 1, 4-structural unit is 10-25 wt%, the content of the 1, 2-structural unit is 50-70 wt%, and the content of the cyclized 1, 2-structural unit is 15-35 wt%. A coating formed by the end group functionalized liquid butadiene polymer shows improved thermal expansion performance, and meanwhile, good adhesive force and adhesion between the liquid butadiene polymer and metal are improved.

Description

Technical Field

[0001] The invention relates to the field of polymers, and in particular to a terminal functionalized liquid butadiene polymer and a preparation method and application thereof, a composition containing the terminal functionalized liquid butadiene polymer and application thereof, and a polymer coating. Background Art

[0002] Liquid butadiene polymer molecular chains contain only carbon-hydrogen structures, have extremely low dielectric constants and dielectric losses, and are widely used in the field of high-frequency electronic circuits. According to microstructural classification, liquid butadiene polymers can be divided into 1,4-addition (cis and trans isomers) and 1,2-addition products. Among 1,2-addition products, they can be divided into medium-vinyl liquid butadiene polymers and high-vinyl liquid butadiene polymers according to the vinyl content. Common high-cis liquid butadiene polymers and low-cis low-vinyl liquid butadiene polymers have high photo (or thermal) cross-linking reaction activity and poor mechanical properties after curing because most of the double bonds are located in the main chain.

[0003] High vinyl liquid butadiene polymer refers to a liquid butadiene polymer with a 1,2-structure content greater than 65%. Since most of the double bonds are located in the side chains of the molecules, the photo (or thermal) cross-linking reaction activity is high and the photo (or thermal) curing is convenient. However, the heat resistance of the coating formed after curing and the adhesion to the metal surface are not satisfactory.

[0004] CN113698520A discloses a liquid butadiene polymer with a number average molecular weight of 2500-5500, a molecular weight distribution of 1-1.2, and a vinyl content of 85-95%. The liquid butadiene polymer has a low dielectric constant, dielectric loss and film-forming properties, but the heat resistance and adhesion to metal are not satisfactory. CN114106228A discloses a method for preparing a liquid butadiene polymer and its product, which can meet the cross-linking and curing activity requirements of the high-end electronic industry, but also cannot solve the problems of heat resistance and adhesion and bonding to metal.

[0005] Therefore, it is of great significance to improve the heat resistance of liquid butadiene polymer, solve the adhesion and bonding between liquid butadiene polymer and metal, and meet the rapid development of high-frequency communication technology. Summary of the invention

[0006] In view of the technical problems that the liquid butadiene polymer prepared by the prior art has a relatively high thermal expansion coefficient and unsatisfactory adhesion and bonding to metals, the inventors of the present invention have conducted in-depth research on the anionic polymerization process of liquid butadiene polymers and developed an end-functionalized liquid butadiene polymer. The coating formed by the end-functionalized liquid butadiene polymer shows improved thermal expansion performance, while improving the good adhesion and bonding to metals of the liquid butadiene polymer, thereby completing the present invention.

[0007] In order to achieve the above-mentioned object, the present invention provides an end-functionalized liquid butadiene polymer on the one hand, wherein the end-capping efficiency of the end-functionalized liquid butadiene polymer is 0.8-1; based on the total weight of the liquid butadiene polymer, the content of 1,4-structural units is 10 weight %-25 weight %, the content of 1,2-structural units is 50 weight %-70 weight %, and the content of cyclized 1,2-structural units is 15 weight %-35 weight %.

[0008] A second aspect of the present invention provides a method for preparing an end-functionalized liquid butadiene polymer, wherein the method comprises:

[0009] (1) in the presence of a solvent, a structure regulator and an initiator, continuously adding 1,3-butadiene monomer into a reactor to carry out anionic solution polymerization reaction to obtain a polymerization reaction solution containing butadiene polymer; wherein the butadiene monomer is continuously polymerized at a temperature of 60-100° C., the structure regulator comprises component A and component B, the component A is a tertiary amine, the component B is an alkali metal alkoxide, the molar ratio of the component B to the component A is 0.1-0.5:1, and the solvent comprises an aliphatic heterocyclic solvent;

[0010] (2) After the product obtained in step (1) is contacted with an alkyl aluminum compound, a functionalizing agent is added to carry out an end-capping reaction to obtain an end-functionalized liquid butadiene polymer; wherein the molar ratio of the alkyl aluminum compound to the initiator is 0.5-1.5:1.

[0011] The third aspect of the present invention provides a terminal functionalized liquid butadiene polymer prepared by the above method.

[0012] The fourth aspect of the present invention provides a composition, which comprises a terminal functionalized liquid butadiene polymer and at least one additive, wherein the terminal functionalized liquid butadiene polymer is the terminal functionalized liquid butadiene polymer described above.

[0013] A fifth aspect of the present invention provides a polymer coating, which contains the above-mentioned terminal functionalized liquid butadiene polymer or the above-mentioned composition.

[0014] A sixth aspect of the present invention provides a use of the terminal functionalized liquid butadiene polymer or the composition as a crosslinking agent, an adhesive or an electrical insulating material.

[0015] Through the above technical scheme, the terminal functionalized liquid butadiene polymer provided by the present invention has good performance. The coating formed by the terminal functionalized high vinyl cyclized liquid butadiene polymer not only has high peel strength and improved thermal expansion performance for the metal substrate, but also has strong bonding force between the coatings, and has broad application prospects in the field of communication technology. DETAILED DESCRIPTION

[0016] The endpoints and any values ​​of the ranges disclosed in this article are not limited to the precise ranges or values, and these ranges or values ​​should be understood to include values ​​close to these ranges or values. For numerical ranges, the endpoint values ​​of each range, the endpoint values ​​of each range and the individual point values, and the individual point values ​​can be combined with each other to obtain one or more new numerical ranges, which should be considered as specifically disclosed in this article.

[0017] In the present invention, the term "liquid butadiene polymer" refers to a butadiene polymer having fluidity at 25°C and 1 standard atmospheric pressure.

[0018] In the present invention, the term "1,2-structural unit" refers to a structural unit formed by 1,3-butadiene in a 1,2-polymerization manner, and the content of 1,2-structural units may also be referred to as vinyl content. In the present invention, the content of 1,2-structural units in the polymer is determined by nuclear magnetic resonance spectroscopy.

[0019] In the present invention, the term "cyclized 1,2-structural unit" refers to the vinyl groups in two adjacent 1,2-structural units bonded to form a five-membered ring, and the specific structure is shown below:

[0020]

[0021] In the present invention, the content of cyclized 1,2-structural units in the polymer is determined by nuclear magnetic resonance spectroscopy.

[0022] In the present invention, the end-capping rate of the polymer is determined by nuclear magnetic resonance spectroscopy.

[0023] In the present invention, the specific test method of nuclear magnetic resonance spectroscopy is: using a Bruker AVANCE400 superconducting nuclear magnetic resonance wave instrument ( 1 H-NMR) test, 1The resonance frequency of the H nucleus is 400.13 MHz, the spectral width is 2747.253 Hz, the pulse width is 5.0 μs, the data point is 16 K, the sample tube diameter is 5 mm, the solvent is deuterated chloroform (CDCl3), the sample concentration is 15% (mg / mL), the test temperature is room temperature (25°C), the number of scans is 16 times, and the chemical shift of tetramethylsilane is calibrated to 0 ppm.

[0024] In the present invention, molecular weight and molecular weight distribution index (M w / M n ) was determined by gel permeation chromatography. The specific test method was: using HLC-8320 gel permeation chromatograph produced by Tosoh Corporation of Japan, the chromatographic column was TSKgelSuperMultiporeHZ-N, the standard column was TSKgel SuperMultiporeHZ, the solvent was chromatographic pure tetrahydrofuran (THF), and narrow distribution polystyrene was used as the standard sample. The polymer sample was prepared into a tetrahydrofuran solution with a concentration of 1 mg / mL, the injection volume was 10.00 μL, the flow rate was 0.35 mL / min, and the test temperature was 40.0°C.

[0025] In the present invention, the content of metal elements in the polymer is determined by plasma method, and the specific test method is: using the Optima 8300 full-spectrum direct-reading ICP spectrometer of PerkinElmer (PE) of the United States, equipped with a medium-step grating, a solid-state detector, a dual-path dual solid-state detector in the ultraviolet light region and the visible light region, and using flat-panel plasma technology; the instrument operating parameters are as follows: high-frequency power 1300W, plasma gas flow 15L / min, atomizing gas flow 0.55L / min, auxiliary gas flow 0.2L / min, peristaltic pump speed 1.50mL / min, integration time 10s, plasma axial observation. The sample preparation method is as follows: accurately weigh 2.000g of the sample in a porcelain crucible, place it in a high-temperature resistance furnace and gradually heat it to 500℃, take it out after complete ashing, add 5mL of 10 volume % dilute nitric acid, slowly heat it on a hot plate until it is completely dissolved, evaporate the solution to dryness, add 1mL of concentrated nitric acid, transfer it to a 50mL volumetric flask, and make up to volume with water, and prepare a reagent blank solution at the same time.

[0026] In the present invention, the linear thermal expansion coefficient is measured by thermomechanical analysis (TMA) according to the method specified in GB / T 36800.2-2018.

[0027] In the present invention, the peel strength between the polymer coating and the metal substrate (copper foil) is tested using the method specified in IPC-TM-650.

[0028] In the present invention, the interlayer bonding strength of the metal substrate after the polymer coating is cured is tested according to the DB44T1088-2012 standard.

[0029] The first aspect of the present invention provides an end-functionalized liquid butadiene polymer, wherein the end-capping efficiency of the end-functionalized liquid butadiene polymer is 0.8-1; based on the total weight of the liquid butadiene polymer, the content of 1,4-structural units is 10% by weight to 25% by weight, the content of 1,2-structural units is 50% by weight to 70% by weight, and the content of cyclized 1,2-structural units is 15% by weight to 35% by weight.

[0030] According to the present invention, the end-capping efficiency of the terminal functionalized liquid butadiene polymer is 0.8-1, for example, it can be 0.8, 0.81, 0.82, 0.83, 0.84, 0.85, 0.86, 0.87, 0.88, 0.89, 0.9, 0.91, 0.92, 0.93, 0.94, 0.95, 0.97, 0.98, 0.99 or 1. Preferably, the end-capping efficiency of the terminal functionalized liquid butadiene polymer is 0.9-1, preferably 0.95-1. In the present invention, the terminal functionalized liquid butadiene polymer has a high end-capping efficiency, and after being used as a coating, it has improved adhesion to the metal substrate.

[0031] According to the present invention, based on the total weight of the terminal functionalized liquid butadiene polymer, the 1,4-structural unit content is 10 wt%-25 wt%, for example, it can be 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24 or 25 wt%. Preferably, based on the total amount of the high vinyl cyclized liquid butadiene polymer, the 1,4-structural unit content is 10 wt%-20 wt%. When the 1,4-structural unit content is less than 10 wt%, it is necessary to carry out at a lower temperature, which affects the cyclized structural unit content of the polymer; when the 1,4-structural unit content is greater than 25 wt%, the double bonds that can participate in the curing crosslinking are reduced, the crosslinking density of the polymer coating prepared from the polymer is reduced, and the mechanical properties are deteriorated.

[0032] According to the present invention, based on the total weight of the terminal functionalized liquid butadiene polymer, the content of 1,2-structural units is 50 wt%-70 wt%, for example, it can be 50, 51, 52, 53, 54, 55, 56, 57, 58, 59, 60, 61, 62, 63, 64, 65, 66, 67, 68, 69 or 70 wt%. Preferably, based on the total weight of the terminal functionalized liquid butadiene polymer, the content of 1,2-structural units is 50 wt%-65 wt%. More preferably, based on the total weight of the terminal functionalized liquid butadiene polymer, the content of 1,2-structural units is 52 wt%-62 wt%. If the content of 1,2-structural units is less than 50 wt%, the crosslinking density of the polymer coating prepared from the polymer is reduced, and the mechanical properties are deteriorated; if the content of 1,2-structural units is greater than 70 wt%, the content of cyclized 1,2-structural units is reduced, which is not conducive to the improvement of the thermal expansion coefficient.

[0033] According to the present invention, based on the total weight of the terminal functionalized liquid butadiene polymer, the content of cyclized 1,2-structural units is 15 wt%-35 wt%, for example, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34 or 35 wt%. Preferably, based on the total weight of the terminal functionalized liquid butadiene polymer, the content of cyclized 1,2-structural units is 18 wt%-35 wt%. More preferably, based on the total weight of the terminal functionalized liquid butadiene polymer, the content of cyclized 1,2-structural units is 20 wt%-35 wt%. In the present invention, if the content of cyclized 1,2-structural units is less than 15% by weight, the thermal expansion coefficient of the coating after curing is not significantly improved; if the content of cyclized 1,2-structural units is greater than 35% by weight, in order to prepare liquid polybutadiene rubber with a higher cyclized structure content, increasing the polymerization temperature becomes the only option, which is not conducive to increasing the total 1,2-structure content of the polymer, and the peel strength between the coating formed by the polymer and the metal substrate decreases, and the interlayer bonding force between copper foils decreases after the polymer coating is cured.

[0034] According to the present invention, in the terminal functionalized high vinyl liquid butadiene polymer, the molar ratio of the cyclized 1,2-structural unit to the 1,2-structural unit is preferably 0.2-0.7: 1, more preferably 0.3-0.6: 1. In the present invention, when the molar ratio of the cyclized 1,2-structural unit to the 1,2-structural unit in the liquid butadiene polymer meets the above range, the comprehensive performance of the polymer coating after curing is better.

[0035] According to the present invention, the number average molecular weight (M) of the terminal functionalized liquid butadiene polymer is n) can be 3500-10000 g / mol, preferably 4500-8000 g / mol.

[0036] In the present invention, the terminal functionalized liquid butadiene polymer not only has a molecular weight suitable for molding, but also has a narrow molecular weight distribution. Generally, according to the present invention, the molecular weight distribution index (M w / M n ) can be 1-1.2, preferably 1-1.15.

[0037] According to the present invention, based on the total weight of the terminal functionalized liquid butadiene polymer, the weight content of the metal element in the liquid butadiene polymer is 200 ppm or less, preferably 100 ppm or less, more preferably 50 ppm or less, and further preferably 20 ppm or less. Controlling the metal content in the polymer is conducive to reducing the dielectric constant and dielectric loss of the cross-linked and cured product, thereby obtaining better application in the field of electronic communications.

[0038] According to the present invention, the linear thermal expansion coefficient of the terminal functionalized liquid butadiene polymer after curing is 40×10 -6 m / m / ℃-75×10 -6 m / m / ℃, preferably 45×10 -6 m / m / ℃-70×10 -6 m / m / ℃, more preferably 50-70×10 -6 m / m / ℃.

[0039] According to the present invention, the peel strength between the coating formed by the terminal functionalized liquid butadiene polymer and the metal substrate (such as copper foil) is 0.9-1.2 N / mm, preferably 1.01-1.2 N / mm, and more preferably 1.08-1.2 N / mm.

[0040] According to the present invention, after the coating formed by the terminal functionalized liquid butadiene polymer is cured, the interlayer bonding force of the metal substrate is 0.8-1.1 N / mm, preferably 0.92-1.1 N / mm, and more preferably 0.95-1.1 N / mm.

[0041] The third aspect of the present invention provides a method for preparing an end-functionalized liquid butadiene polymer, the method comprising:

[0042] (1) in the presence of a solvent, a structure regulator and an initiator, continuously adding 1,3-butadiene monomer into a reactor for anionic solution polymerization to obtain a polymerization solution containing high vinyl cyclized liquid butadiene, wherein the contact is carried out at a temperature of 60-100° C., the structure regulator comprises component A and component B, the component A is a tertiary amine, the component B is an alkali metal alcohol salt, the molar ratio of the component B to the component A is 0.1-0.5:1, and the solvent comprises an aliphatic heterocyclic solvent;

[0043] (2) After the product obtained in step (1) is contacted with an alkyl aluminum compound, a functionalizing agent is added to carry out an end-capping reaction to obtain an end-functionalized liquid butadiene polymer; wherein the molar ratio of the alkyl aluminum compound to the initiator is 0.5-1.5:1.

[0044] In the present invention, the term “continuously” means that the 1,3-butadiene monomer required for polymerization is added gradually and continuously into the reactor, rather than adding all the 1,3-butadiene monomer required for polymerization into the reactor at one time.

[0045] In the present invention, by continuously adding the 1,3-butadiene monomer required for polymerization into the reactor, the polymerization reaction can be precisely controlled, ensuring that the active species of the initiator are always in a hungry state, which is more conducive to the formation of the 1,2-cyclized structure. Further, the content of the cyclized 1,2-structure in the liquid butadiene polymer is increased, and the liquid butadiene polymer with a high cyclized 1,2-structure content is contacted with an alkyl aluminum compound and then end-capped with a functionalizing agent to obtain the end-functionalized liquid butadiene polymer described in the first aspect of the present invention. In particular, when the molar ratio of the alkyl aluminum compound to the initiator is controlled to meet the above range, the end-capping efficiency of the functionalizing agent can be significantly improved.

[0046] In the present invention, the 1,4-structural unit content, the 1,2-structural unit content and the cyclized 1,2-structural unit content in the terminal functionalized liquid butene polymer are determined by step (1), and the end-capping reaction does not affect the 1,4-structural unit content, the 1,2-structural unit content and the cyclized 1,2-structural unit content in the liquid butene polymer.

[0047] Furthermore, the molar ratio of the alkyl aluminum compound to the initiator is 0.8-1.2:1.

[0048] According to the present invention, the contact time is 1-10 min, preferably 2-8 min.

[0049] According to the present invention, the alkyl aluminum compound is at least one selected from trimethyl aluminum, triethyl aluminum, tripropyl aluminum, triisopropyl aluminum, tributyl aluminum and triisobutyl aluminum.

[0050] According to the present invention, the functionalizing agent is selected from imine compounds, preferably at least one selected from N-benzylidene-3-triethoxysilyl-1-propylamine, N-N'-p-dimethylbenzylidene-3-ethoxysilyl-1-propylamine, N-N'-p-diethylbenzylidene-3-ethoxysilyl-1-propylamine and N-benzylidene-3-trimethoxyethoxy-1-propylamine.

[0051] In the present invention, the above-mentioned specific type of functionalizing agent is used to end-cap the butadiene polymer containing a cyclized 1,2-structure. Since the end-capping agent contains more polar functional groups, the peel strength between the polymer and the metal substrate can be significantly improved.

[0052] According to the present invention, the molar ratio of the functionalizing agent to the initiator is 1-1.1:1.

[0053] In the present invention, when the molar ratio of the functionalizing agent to the initiator is controlled to meet the above range, it is ensured to have the functionalizing end-capping agent on each molecular chain of the polymer to the greatest extent, and the side reaction of the functionalizing agent is reduced.

[0054] Furthermore, the molar ratio of the functionalizing agent to the initiator is 1-1.05:1.

[0055] According to the present invention, the temperature of the end-capping reaction is 30-80° C., and the time of the end-capping reaction is 20-60 min.

[0056] According to the present invention, based on 100 g of solvent, the rate of adding 1,3-butadiene into the reactor is 0.1-0.5 g / min, preferably 0.15-0.35 g / min.

[0057] According to the present invention, butadiene monomer is continuously reacted at a temperature of 60°C to 90°C, preferably 70°C to 90°C.

[0058] In the present invention, the anionic polymerization reaction can be carried out under a pressure of 0.005-1.5MPa, more preferably under a pressure of 0.1-1MPa, and further preferably under a pressure of 0.2-0.6MPa. In the present invention, pressure refers to gauge pressure. The polymerization time can be selected according to the final monomer concentration and polymerization temperature of the polymerization reaction, and can generally be 30-120min, preferably 40-80min.

[0059] In the present invention, the anionic polymerization reaction is carried out in an atmosphere formed by an inert gas. The inert gas refers to a gas that does not chemically interact with reactants, reaction products and solvents under polymerization conditions, such as nitrogen and / or zero group element gas (such as argon).

[0060] In a preferred embodiment, the component A is one or more compounds selected from the group consisting of compounds shown in formula I.

[0061]

[0062] In formula I, R2 and R3 are the same or different and are each independently a C1-C6 alkyl group.

[0063] In formula I, R1 is a monovalent group shown in formula II,

[0064]

[0065] In Formula II, m is an integer of 1-5, for example, 1, 2, 3, 4 or 5.

[0066] In formula II, R4 and R5 are the same or different and are independently a hydrogen atom or a C1-C6 alkyl group, preferably a hydrogen atom.

[0067] In formula II, R6 is -NR7R8, or a C3-C6 oxacycloalkyl group, and R7 and R8 are the same or different and are each independently a C1-C6 alkyl group.

[0068] In Formula I and Formula II, the C1-C6 alkyl group includes a C1-C6 straight-chain alkyl group and a C3-C6 branched-chain alkyl group, and specific examples thereof may include, but are not limited to, methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl, tert-pentyl, neopentyl and n-hexyl.

[0069] In a preferred embodiment of the present invention, the component A is N,N,N',N'-tetramethylethylenediamine and / or N,N-dimethyltetrahydrofurfurylamine. In a particularly preferred embodiment, the component A is N,N,N',N'-tetramethylethylenediamine.

[0070] In a preferred embodiment of the present invention, the component B is one or more compounds selected from the group consisting of compounds represented by formula III.

[0071] R9-O-M1 (Formula III)

[0072] In formula III, R9 is C1-C 20 Alkyl, C1-C 20 Alkyl or C6-C 30 The aromatic group,

[0073] M1 is an alkali metal atom, such as Li, Na or K, preferably Na.

[0074] In Formula III, C1-C 20 The alkyl groups include C1-C20 Straight chain alkyl and C3-C 20 Specific examples of the branched alkyl group may include, but are not limited to, methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, tert-butyl, n-pentyl and its isomers, n-hexyl and its isomers, n-heptyl and its isomers, n-octyl and its isomers, n-nonyl and its isomers, n-decyl and its isomers, undecyl and its isomers, dodecyl and its isomers, tridecyl and its isomers, tetradecyl and its isomers, pentadecyl and its isomers, hexadecyl and its isomers, heptadecyl and its isomers, octadecyl and its isomers, nonadecyl and its isomers, and eicosyl and its isomers.

[0075] In Formula III, the C1-C 20 The substituent in the alkyl group is preferably a cycloalkyl group containing a heteroatom, and specific examples of the heteroatom may include, but are not limited to, an oxygen atom, a sulfur atom or a nitrogen atom. In a preferred embodiment, the heteroatom in the substituent containing a heteroatom is an oxygen atom, and the substituent containing a heteroatom is a cycloalkyl group containing an oxygen atom, for example: an ethylene oxide substituent, a propylene oxide substituent, a propylene oxide substituent, a tetrahydrofuran substituent, or an oxirane substituent.

[0076] In Formula III, C6-C 30 Specific examples of the aryl group may include, but are not limited to, phenyl, o-tolyl, m-tolyl, p-tolyl, o-ethylphenyl, m-ethylphenyl, p-ethylphenyl, o-tert-butylphenyl, m-tert-butylphenyl, p-tert-butylphenyl, p-dodecylphenyl, 2,4-di-n-butylphenyl, p-n-propylphenyl, and 2,4-diethylphenyl.

[0077] In a preferred embodiment of the present invention, the component B is preferably one or more of sodium tetrahydrofurfuryl alcohol, sodium tert-amyl oxide, sodium tert-butoxylate, sodium n-hexoxide and sodium menthol.

[0078] In a preferred embodiment of the present invention, the molar ratio of the component B to the component A is 0.1-0.5:1, preferably 0.15-0.45:1, and more preferably 0.2-0.4:1.

[0079] In a preferred embodiment of the present invention, the amount of the structure regulator can be adjusted according to the amount of the monomer and / or the anionic polymerization initiator. Relative to 1 mol of the anionic polymerization initiator, the amount of the component A can be 0.5-2 mol, preferably 0.7-1.5 mol. Relative to 1 mol of the anionic polymerization initiator, the amount of the component B can be 0.1-0.5 mol, preferably 0.2-0.4 mol.

[0080] In a preferred embodiment of the present invention, the anionic polymerization initiator is preferably an organic lithium initiator, more preferably an organic monolithium compound, and further preferably a compound represented by formula IV,

[0081] R 10 Li (Formula IV)

[0082] In Formula IV, R 10 C1-C6 alkyl, C3-C 12 Cycloalkyl, C7-C 14 Arylalkyl or C6-C 12 The aromatic group.

[0083] In formula IV, the C1-C6 alkyl group includes C1-C6 straight-chain alkyl groups and C3-C6 branched-chain alkyl groups, and specific examples thereof may include, but are not limited to, methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl, tert-pentyl, neopentyl and n-hexyl.

[0084] In Formula IV, C3-C 12 Specific examples of the cycloalkyl group may include, but are not limited to, cyclopropyl, cyclopentyl, cyclohexyl, 4-methylcyclohexyl, 4-ethylcyclohexyl, 4-n-propylcyclohexyl, and 4-n-butylcyclohexyl.

[0085] In Formula IV, C7-C 14 Specific examples of the aralkyl group may include, but are not limited to, phenylmethyl, phenylethyl, phenyl-n-propyl, phenyl-n-butyl, phenyl-t-butyl, phenyl-isopropyl, phenyl-n-pentyl, and phenyl-n-butyl.

[0086] In Formula IV, C6-C 12 Specific examples of the aryl group may include, but are not limited to, phenyl, naphthyl, 4-methylphenyl, and 4-ethylphenyl.

[0087] In the present invention, specific examples of the anionic polymerization initiator may include, but are not limited to, one or more of ethyl lithium, n-propyl lithium, isopropyl lithium, n-butyl lithium, sec-butyl lithium, tert-butyl lithium, phenyl lithium, 2-naphthyl lithium, 4-butylphenyl lithium, 4-tolyl lithium, cyclohexyl lithium and 4-butylcyclohexyl lithium. Preferably, the anionic polymerization initiator is n-butyl lithium and / or sec-butyl lithium, and more preferably, the anionic polymerization initiator is n-butyl lithium.

[0088] In the present invention, the amount of the anionic polymerization initiator can be selected according to the molecular weight of the expected end-functionalized liquid butadiene polymer. Preferably, the amount of the anionic polymerization initiator is such that the number average molecular weight of the prepared liquid butadiene polymer is 3500-10000 g / mol, preferably 4500-8000 g / mol. The method for determining the specific amount of the anionic polymerization initiator according to the expected polymer molecular weight is well known to those skilled in the art and will not be described in detail herein.

[0089] According to the present invention, the solvent contains an aliphatic heterocyclic solvent. The term "aliphatic heterocyclic" refers to a cycloalkane in which at least one carbon atom on the ring is replaced by a heteroatom. The heteroatom in the aliphatic heterocyclic ring can be an oxygen atom, a nitrogen atom or a sulfur atom, preferably an oxygen atom. The solvent can be one or more selected from tetrahydrofuran, cyclopentane oxide, cyclohexane oxide and 1,4-dioxane. The solvent can be used alone or in combination. In a preferred embodiment, the solvent is an aliphatic heterocyclic solvent, more preferably an oxacycloalkane. In a particularly preferred embodiment, the solvent is tetrahydrofuran.

[0090] In the present invention, the content of 1,3-butadiene monomer can be 1-40% by weight, preferably 10-30% by weight, based on the total weight of the solvent and the 1,3-butadiene monomer. In the present invention, the monomer content refers to the total weight percentage of 1,3-butadiene monomer determined based on the total weight of the solvent and the 1,3-butadiene monomer after the polymerization reaction.

[0091] In the present invention, the preparation method further comprises: after the end-capping reaction is completed, adding a terminator, removing the organic lithium initiator and the solvent, and obtaining the terminal functionalized liquid butadiene polymer.

[0092] In the present invention, there is no particular limitation on the type and amount of the terminator, and conventional terminators in the art may be used and added in conventional amounts in the art.

[0093] In the present invention, the preparation method may further include: removing at least part of the metal ions in the polymerization reaction mixture to obtain a purified polymerization reaction mixture. The polymerization reaction mixture may be washed to remove at least part of the metal ions.

[0094] In a preferred embodiment, the method for removing at least part of the metal ions in the polymerization mixture comprises: mixing the polymerization mixture with a washing liquid, and separating the oil phase from the mixture, wherein the washing liquid is water or an aqueous solution containing an acid. In this preferred embodiment, the acid is preferably an inorganic acid, more preferably one or more of sulfuric acid, nitric acid, hydrochloric acid and carbonic acid. When the acid is carbonic acid, carbonic acid can be formed by passing carbon dioxide gas into the mixture of the polymerization mixture and water and / or adding dry ice to the polymerization mixture.

[0095] In a more preferred example of this preferred embodiment, the washing liquid includes a first washing liquid and a second washing liquid, the first washing liquid is an aqueous solution containing acid I, the second aqueous solution is an aqueous solution containing acid II, the acid I is one or more of sulfuric acid, hydrochloric acid and nitric acid, and the acid II is carbonic acid, and the method for removing at least part of the metal ions in the polymerization reaction mixture comprises: mixing the polymerization reaction mixture with the first washing liquid to obtain a first mixture, separating a first oil phase from the first mixture, removing at least part of the solvent in the first oil phase, and obtaining a crude product of liquid butadiene polymer; in the presence of carbon dioxide, mixing the first oil phase with water to obtain a second mixture, separating a second oil phase from the second mixture, removing at least part of the volatile components in the second oil phase, and obtaining a liquid butadiene polymer. In this more preferred example, the weight ratio of the first washing liquid to the monomer is preferably 1-5:1, more preferably 2-4:1, the molar ratio of the acid I in the first washing liquid to the anionic polymerization initiator is preferably 0.5-3:1, more preferably 1-2:1, and the acid I is in the form of H + The weight ratio of the second washing liquid to the monomer is 1-2: 1, the molar ratio of the acid II in the second washing liquid to the anionic polymerization initiator is preferably 0.1-1.5: 1, the acid II to H + count.

[0096] In the present invention, various reagents used in the preparation method are preferably refined by conventional methods in the art before use to remove impurities (especially water) therein. The method for refining the reagents is well known in the art and will not be described in detail herein.

[0097] In the present invention, the anionic solution polymerization reaction can be carried out by batch polymerization or continuous polymerization, without particular limitation.

[0098] The third aspect of the present invention provides a terminal functionalized liquid butadiene polymer prepared by the above method.

[0099] The terminal functionalized liquid butadiene polymer prepared by the method described in the second aspect of the present invention not only has a high 1,2-structural unit content, but also some of the 1,2-structural units form a cyclic structure and contain an ethylene oxide block. The coating formed by the raw material containing the liquid butadiene polymer prepared by the method described in the second aspect of the present invention shows more excellent thermal expansion performance while maintaining high peel strength and interlayer bonding force.

[0100] The fourth aspect of the present invention provides a composition, which comprises a terminal functionalized liquid butadiene polymer and at least one additive, wherein the terminal functionalized liquid butadiene polymer is the terminal functionalized liquid butadiene polymer described above.

[0101] In the present invention, the additive can be a substance that can give the composition new properties and / or improve the existing properties of the composition. As a preferred example, the additive contains an antioxidant. The antioxidant can be a conventional selection, for example, the antioxidant can be a phenolic and / or amine antioxidant. Specifically, the antioxidant can be one or more of 4,6-dioctylthiomethyl o-cresol, tetrakis[3-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid] pentaerythritol ester (i.e., antioxidant 264), tris(2,4-di-tert-butylphenyl) phosphite (i.e., antioxidant 168), 3-(3,5-di-tert-butyl-4-hydroxyphenyl) propionic acid octadecyl ester (i.e., antioxidant 1076), 2,6-di-tert-butyl-p-cresol, tert-butylcatechol and 2,2'-methylene-bis(4-methyl-6-tert-butylphenol). The antioxidant may be contained in an amount of 0.005-2 parts by weight, preferably 0.01-1 parts by weight, relative to 100 parts by weight of the liquid butadiene polymer.

[0102] A fifth aspect of the present invention provides a polymer coating, which contains the above-mentioned terminal functionalized liquid butadiene polymer or the above-mentioned composition.

[0103] In the present invention, the polymer coating not only has high adhesion and bonding to the substrate, but also has a reduced thermal expansion coefficient, showing improved thermal expansion performance.

[0104] A sixth aspect of the present invention provides a use of the terminal functionalized liquid butadiene polymer or the composition as a crosslinking agent, an adhesive or an electrical insulating material.

[0105] The present invention will be described in detail below with reference to the embodiments, but the scope of the present invention is not limited thereby.

[0106] Unless otherwise specified, normal temperature and room temperature both refer to 25±3℃.

[0107] In the following examples and comparative examples, the microstructure of the polymer was measured using a Bruker AVANCE400 superconducting nuclear magnetic resonance instrument ( 1 H-NMR) determination, 1 The resonance frequency of the H nucleus is 400.13 MHz, the spectral width is 2747.253 Hz, the pulse width is 5.0 μs, the data point is 16 K, the sample tube diameter is 5 mm, the solvent is deuterated chloroform (CDCl3), the sample concentration is 15% (W / V), the test temperature is room temperature, the number of scans is 16 times, and the chemical shift is calibrated with tetramethylsilane as 0 ppm.

[0108] In the following examples and comparative examples, the molecular weight and molecular weight distribution index of the polymer were determined by gel permeation chromatography analysis. The gel permeation chromatography analysis was performed using an HLC-8320 gel permeation chromatograph produced by Tosoh Corporation of Japan. The chromatographic column was TSKgel SuperMultiporeHZ-N, the standard column was TSKgel SuperMultiporeHZ, the solvent was chromatographically pure tetrahydrofuran (THF), and narrow distribution polystyrene was used as the standard sample. The polymer sample was prepared into a tetrahydrofuran solution with a mass concentration of 1 mg / mL, the injection volume was 10.00 μL, the flow rate was 0.35 mL / min, and the test temperature was 40.0°C.

[0109] In the following examples and comparative examples, the linear thermal expansion coefficient is measured by thermomechanical analysis (TMA) according to the method specified in GB / T 36800.2-2018.

[0110] In the following examples and comparative examples, the peel strength between the polymer coating and the copper foil was tested using the method specified in IPC-TM-650 2.4.08C.

[0111] In the following examples and comparative examples, the interlayer bonding strength of the copper foil is tested according to the DB44T1088-2012 standard.

[0112] In the following examples and comparative examples, the following chemical reagents are involved:

[0113] Antioxidant 264, antioxidant 168, and antioxidant 1076 were purchased from Sinopharm Reagent Company;

[0114] Tetrahydrofuran: chromatographically pure, soaked on molecular weight sieves for 15 days, water content less than 5ppm (weight content).

[0115] 1,3-Butadiene: polymerization grade, purchased from Yanshan Petrochemical.

[0116] n-Butyl lithium: purchased from J&K Reagent Company, as a 1.6 mol / L hexane solution.

[0117] 2,2-Di(2-tetrahydrofuryl)propane) (DTHFP): purchased from J&K Reagent Co., analytical grade.

[0118] N,N,N',N'-Tetramethylethylenediamine (TMEDA): purchased from J&K Reagent Co., analytical grade.

[0119] Sodium tert-amyloxide (STA): purchased from J&K Reagent Company, 1.4 mol / L tetrahydrofuran solution.

[0120] Sodium tetrahydrofurfuryl alcohol (THFOA): purchased from Inotech Reagent Company, 1.0 mol / L tetrahydrofuran solution.

[0121] Sodium menthol (SMT): purchased from Inotech Reagent Company, 1.0 mol / L tetrahydrofuran solution.

[0122] N-Benzylidene-3-triethoxysilyl-1-propylamine (TEOS): purchased from Qingkai Huafeng Reagent Company, purity>95%.

[0123] N-N'-p-Dimethylbenzylidene-3-ethoxysilyl-1-propylamine (DETOS): purchased from Qingkai Huafeng Reagent Company, purity>95%.

[0124] Triisobutylaluminum (Al): purchased from Inotech Reagent Company, 1 mol / L hexane solution.

[0125] Sulfuric acid: purchased from J&K Reagent Company, concentration is 98 wt%, prepared with water to make a 20 wt% solution.

[0126] Nitric acid: purchased from Sinopharm Reagent Company, with a concentration of 68% by weight, prepared with water to a 20% by weight solution.

[0127] Example 1

[0128] This example is used to illustrate the terminal functionalized liquid butadiene polymer and the preparation method thereof of the present invention.

[0129] (1) Under nitrogen protection, tetrahydrofuran (THF), structure regulator 1, structure regulator 2, and n-butyl lithium (types and amounts are shown in Table 1, and the amounts listed in Table 1 are all measured based on pure compounds) are added to a 5 L reactor, the temperature in the reactor is controlled to be the polymerization reaction temperature listed in Table 1, and 1,3-butadiene monomer is continuously added to the reactor (the addition rate and time are shown in Table 1, and the amounts listed in Table 1 are all measured based on pure compounds); and anionic solution polymerization is carried out at the temperature and pressure listed in Table 1 to obtain a polymerization reaction mixture of a liquid butadiene polymer.

[0130] (2) Adding a designed amount of an alkyl aluminum compound (the type and amount are shown in Table 1, and the amounts listed in Table 1 are all measured based on pure compounds) to the liquid butadiene polymer reaction mixture obtained in step (1), adding a designed amount of a functionalizing agent for end-capping (the type and amount are shown in Table 1, and the amounts listed in Table 1 are all measured based on pure compounds) after the reaction is completed, and conducting an anionic solution polymerization reaction at the temperature and pressure listed in Table 1 to obtain an end-functionalized liquid butadiene polymer reaction solution.

[0131] (3) Add water and acid (the specific amounts and types of acids are listed in Table 2, and the amounts listed in Table 2 are all measured based on pure compounds) to the polymerization reaction mixture obtained in step (2), stir for 15 minutes, and then stand for stratification to separate the aqueous phase. The obtained oil phase is subjected to reduced pressure distillation to obtain a crude end-functionalized liquid butadiene polymer.

[0132] (4) Add water to the crude liquid polybutadiene obtained in step (3), and introduce carbon dioxide gas with stirring (the specific amounts of water and carbon dioxide are listed in Table 2), then stand for stratification to separate the aqueous phase, subject the obtained oil phase to reduced pressure distillation, and add an antioxidant to the distillation residue (the specific amount and type are listed in Table 2) to obtain a composition LPB1 containing an end-functionalized liquid butadiene polymer, wherein the structural property parameters of the end-functionalized liquid butadiene polymer are listed in Table 3.

[0133] Embodiment 2-10

[0134] Examples 2-10 are used to illustrate the terminal functionalized liquid butadiene polymers and the preparation methods thereof of the present invention.

[0135] Example 2-10 uses the same method as Example 1 to prepare end-functionalized liquid butadiene polymers, except that step (1) and step (2) are reacted under the conditions shown in Table 1, and step (3) and step (4) are used to treat the polymerization reaction mixture containing butadiene polymer obtained in step (1) under the conditions shown in Table 2, thereby respectively obtaining compositions LPB2-LPB10 containing end-functionalized liquid butadiene polymers, wherein the structural property parameters of the end-functionalized liquid butadiene polymers are listed in Table 3.

[0136] Comparative Example 1

[0137] The same method as in Example 1 was used to prepare a terminal functionalized liquid butadiene polymer, except that no alkyl aluminum was added in step (2). The terminal functionalized liquid butadiene polymer DLPB1 was obtained, and its structural property parameters are listed in Table 3.

[0138] Comparative Example 2

[0139] The liquid butadiene polymer was prepared in the same manner as in Example 1, except that alkyl aluminum and functionalizing agent were not added, to obtain a composition DLPB2 containing a liquid butadiene polymer, wherein the structural property parameters of the liquid butadiene polymer are listed in Table 3.

[0140] Comparative Example 3

[0141] The terminal functionalized liquid butadiene polymer was prepared by the same method as in Example 1, except that the molar ratio of alkyl aluminum to initiator butyl lithium was 0.2, and a composition DLPB3 containing the terminal functionalized liquid butadiene polymer was obtained, and its structural property parameters are listed in Table 3.

[0142] Comparative Example 4

[0143] The liquid butadiene polymer was prepared by the same method as in Example 1, except that in step (1), an equal amount of cyclohexane was used instead of THF as the solvent, an equal amount of DTHFP was used instead of TMEDA, and the polymerization temperature was 10°C to obtain a composition LDPB4 containing a liquid butadiene polymer, wherein the structural property parameters of the liquid butadiene polymer are listed in Table 3.

[0144] Table 1

[0145]

[0146]

[0147] a Based on 100g solvent, Table 1 continued

[0148]

[0149] a Based on 100g solvent

[0150] Table 2

[0151]

[0152] b Relative to 100g of liquid butadiene polymer

[0153] Table 3

[0154]

[0155] Note: PB represents polybutadiene block, Mn represents the number average molecular weight of liquid butadiene polymer, Mw / Mn represents the molecular weight distribution of liquid butadiene polymer, 1,2-PB represents the 1,2-structure content of liquid butadiene polymer, C-1,2-PB represents the cyclized 1,2-structure content of liquid butadiene polymer, and 1,4-PB represents the 1,4-structure content of liquid butadiene polymer.

[0156] It can be seen from Table 3 that the terminal functionalized liquid butadiene polymer provided by the present invention has a high 1,2-structural unit content and a cyclized 1,2-structural unit content, a narrow molecular weight distribution, and a capping efficiency of >0.8, and is an ideal adhesive for the high-frequency communication field.

[0157] Test Case

[0158] Compositions LPB1 to LPB10 prepared in Examples 1-10 (wherein the end-functionalized liquid butadiene polymer is 100 g and the antioxidant is 0.16 g) were uniformly coated on the surface of the copper foil with a coating thickness of 0.8 mm. The coating was cross-linked and cured at 120° C. for 2 hours. The peel strength was measured by the method specified in IPC-TM-650 2.4.08C. The interlayer bonding force between the copper foils was tested according to the method specified in DB44T1088-2012. The linear thermal expansion coefficient was measured by thermomechanical analysis (TMA) according to the method specified in GB / T 36800.2-2018. The experimental results are listed in Table 4.

[0159] Test comparison

[0160] The peel strength, interlayer bonding force and thermal expansion coefficient of the compositions DLPB1 to DLPB4 prepared in Comparative Examples 1-4 were measured using the same method as in the test example. The experimental results are listed in Table 4.

[0161] Table 4

[0162]

[0163]

[0164] It can be seen from the results in Table 4 that the polymer coating formed by the terminal functionalized liquid butadiene polymer provided by the present invention has high peeling strength with the copper foil, good interlayer bonding force between the copper foils, and low thermal expansion coefficient.

[0165] The preferred embodiments of the present invention are described in detail above, but the present invention is not limited thereto. Within the technical concept of the present invention, the technical solution of the present invention can be subjected to a variety of simple modifications, including the combination of various technical features in any other suitable manner, and these simple modifications and combinations should also be regarded as the contents disclosed by the present invention and belong to the protection scope of the present invention.

Claims

1. A terminal functionalized liquid butadiene polymer, characterized in that: The end-capping efficiency of the terminal functionalized liquid butadiene polymer is 0.8-1; based on the total weight of the liquid butadiene polymer, the content of 1,4-structural units is 10%-25% by weight, the content of 1,2-structural units is 50%-70% by weight, and the content of cyclized 1,2-structural units is 15%-35% by weight.

2. The end-functionalized liquid butadiene polymer according to claim 1, wherein The end-capping efficiency of the terminal functionalized liquid butadiene polymer is 0.9-1, preferably 0.95-1; Preferably, based on the total weight of the liquid butadiene polymer, the content of 1,4-structural units is 10 wt%-20 wt%; the content of 1,2-structural units is 50-65 wt%, preferably 52 wt%-62 wt%; the content of cyclized 1,2-structural units is 18 wt%-35 wt%, preferably 20 wt%-35 wt%; Preferably, the molar ratio of cyclized 1,2-structural units to 1,2-structural units in the liquid butadiene polymer is 0.2-0.7:1, preferably 0.3-0.6:

1.

3. The end-functionalized liquid butadiene polymer according to claim 1 or 2, wherein The number average molecular weight of the liquid butadiene polymer is 3500-10000 g / mol, preferably 4500-8000 g / mol; the molecular weight distribution index of the liquid butadiene polymer is 1-1.2, preferably 1-1.15; Preferably, based on the total weight of the liquid butadiene polymer, the weight content of the metal element in the liquid butadiene polymer is 200 ppm or less, preferably 100 ppm or less.

4. The end-functionalized liquid butadiene polymer according to any one of claims 1 to 3, wherein The linear thermal expansion coefficient of the terminal functionalized liquid butadiene polymer after curing is 40×10 -6 m / m / ℃-75×10 -6 m / m / ℃, preferably 45×10 -6 m / m / ℃-70×10 -6 m / m / ℃, more preferably 50×10 -6 m / m / ℃-60×10 -6 m / m / ℃; Preferably, the peel strength between the coating formed by the terminal functionalized liquid butadiene polymer and the metal substrate is 0.9-1.2 N / mm, preferably 1.01-1.2 N / mm, and more preferably 1.08-1.2 N / mm; Preferably, after curing, the coating formed by the terminal functionalized liquid butadiene polymer has an interlayer bonding force on the metal substrate of 0.8-1.1 N / mm, preferably 0.92-1.1 N / mm, and more preferably 0.95-1.1 N / mm.

5. A method for preparing an end-functionalized liquid butadiene polymer, characterized in that: The method comprises: (1) in the presence of a solvent, a structure regulator and an initiator, continuously adding 1,3-butadiene monomer into a reactor to carry out anionic solution polymerization reaction to obtain a polymerization reaction solution containing butadiene polymer; wherein the butadiene monomer is continuously polymerized at a temperature of 60-100° C., the structure regulator comprises component A and component B, the component A is a tertiary amine, the component B is an alkali metal alkoxide, the molar ratio of the component B to the component A is 0.1-0.5:1, and the solvent comprises an aliphatic heterocyclic solvent; (2) After the product obtained in step (1) is contacted with an alkyl aluminum compound, a functionalizing agent is added to carry out an end-capping reaction to obtain an end-functionalized liquid butadiene polymer; wherein the molar ratio of the alkyl aluminum compound to the initiator is 0.5-1.5:

1.

6. The method according to claim 5, wherein: The molar ratio of the alkyl aluminum compound to the initiator is 0.8-1.2:1; Preferably, the contact time is 1-10 min, preferably 2-8 min; Preferably, the alkyl aluminum compound is at least one selected from trimethyl aluminum, triethyl aluminum, tripropyl aluminum, triisopropyl aluminum, tributyl aluminum and triisobutyl aluminum.

7. The method according to claim 5 or 6, wherein: The functionalizing agent is selected from imine compounds, preferably at least one selected from N-benzylidene-3-triethoxysilyl-1-propylamine, N-N'-p-dimethylbenzylidene-3-ethoxysilyl-1-propylamine, N-N'-p-diethylbenzylidene-3-ethoxysilyl-1-propylamine and N-benzylidene-3-trimethoxyethoxy-1-propylamine; Preferably, the molar ratio of the functionalizing agent to the initiator is 1-1.1:1, preferably 1-1.05:1; Preferably, the temperature of the end-capping reaction is 30-80° C., and the time of the end-capping reaction is 20-60 min.

8. The method according to any one of claims 5 to 7, wherein: Based on 100 g of solvent, the rate of adding 1,3-butadiene into the reactor is 0.1-0.5 g / min, preferably 0.15-0.35 g / min; Preferably, the butadiene monomer is continuously reacted at a temperature of 60°C to 90°C.

9. The method according to any one of claims 5 to 8, wherein: The component A is one or more compounds selected from the group consisting of: In formula I, R2 and R3 are the same or different and are independently C1-C6 alkyl groups, and R1 is a monovalent group shown in formula II, In formula II, m is an integer of 1-5, R4 and R5 are the same or different, and are independently a hydrogen atom or a C1-C6 alkyl group, R6 is -NR7R8 or a C3-C6 oxacycloalkyl group, R7 and R8 are the same or different, and are independently a C1-C6 alkyl group, Preferably, the component A is N,N,N',N'-tetramethylethylenediamine and / or N,N-dimethyl-tetrahydrofurfurylamine.

10. The method according to any one of claims 5 to 9, wherein: The component B is one or more compounds selected from the group consisting of: R9—O—M1 (Formula III) In formula III, R9 is C1-C 20 Alkyl, C1-C 20 Alkyl, or C6-C 30 The aromatic group, M1 is an alkali metal atom; Preferably, the heteroatom-containing substituent is a heteroatom-containing cycloalkyl group, and the heteroatom is preferably an oxygen atom, a sulfur atom or a nitrogen atom, more preferably an oxygen atom; Preferably, the component B is one or more of sodium tetrahydrofurfuryl alcohol, sodium tert-pentyl alcohol, sodium tert-butyl alcohol, sodium n-hexanolate and sodium menthol.

11. The method according to any one of claims 5 to 10, wherein: The molar ratio of the component B to the component A is 0.15-0.45:1, preferably 0.2-0.4:

1.

12. The method according to any one of claims 5 to 11, wherein: The amount of component B used is 0.1-0.5 mol, preferably 0.2-0.4 mol, relative to 1 mol of the anionic polymerization initiator.

13. The method according to any one of claims 5 to 12, wherein: The amount of the anionic polymerization initiator is such that the number average molecular weight of the prepared terminal functionalized liquid butadiene polymer is 3500-10000 g / mol, preferably 4500-8000 g / mol; Preferably, the anionic polymerization initiator is an organic lithium initiator, preferably one or more selected from the compounds represented by formula IV. R 10 Li (Formula IV) In Formula IV, R 10 C1-C6 alkyl, C3-C 12 Cycloalkyl, C7-C 14 Arylalkyl or C6-C 12 The aromatic group; More preferably, the anionic polymerization initiator is n-butyllithium and / or sec-butyllithium.

14. The method according to any one of claims 5 to 13, wherein: The solvent is an oxacycloalkane, preferably tetrahydrofuran.

15. A terminal functionalized liquid butadiene polymer prepared by the process of any one of claims 5 to 14.

16. A composition comprising a terminal functionalized liquid butadiene polymer and at least one additive, wherein the terminal functionalized liquid butadiene polymer is the terminal functionalized liquid butadiene polymer according to any one of claims 1 to 4 and 15.

17. The composition according to claim 16, wherein The additive contains an antioxidant.

18. A polymer coating comprising the end-functionalized liquid butadiene polymer of any one of claims 1 to 4 and 15, or the composition of claim 16 or 17.

19. Use of the terminal functionalized liquid butadiene polymer according to any one of claims 1 to 4 and 15, or the composition according to claim 16 or 17 as a crosslinking agent, an adhesive or an electrical insulating material.

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