CN116655859A - Amphiphilic polymer with comb-shaped structure and preparation method and application thereof - Google Patents

Amphiphilic polymer with comb-shaped structure and preparation method and application thereof Download PDF

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Publication number
CN116655859A
CN116655859A CN202310628881.0A CN202310628881A CN116655859A CN 116655859 A CN116655859 A CN 116655859A CN 202310628881 A CN202310628881 A CN 202310628881A CN 116655859 A CN116655859 A CN 116655859A
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vinyl
monomer
amphiphilic polymer
solution
initiator
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吴璧耀
陈永康
吕正伟
林东升
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Anhui Xoanons Chemical Co ltd
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Anhui Xoanons Chemical Co ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • 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
    • C08F283/00Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
    • C08F283/06Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
    • C08F283/065Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals on to unsaturated polyethers, polyoxymethylenes or polyacetals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

The invention relates to the technical field of chemical industry, in particular to an amphiphilic polymer with a comb structure, which is prepared by random free radical solution copolymerization of a single-ended vinyl polyether monomer, a vinyl monomer with an acid group, other vinyl monomers and a (methyl) acrylamide monomer with a long-chain alkyl structure under the action of an initiator. Compared with the prior art, the invention has the beneficial effects that: the amphiphilic polymer developed by the invention is used as a dispersing agent, has the effects of good viscosity reduction and high dispersing efficiency in the homogenization of the anode material of the lithium iron (manganese) phosphate battery, and can effectively maintain the stability of the dispersing liquid, thereby greatly reducing the production cost and achieving the purposes of energy conservation and environmental protection.

Description

Amphiphilic polymer with comb-shaped structure and preparation method and application thereof
Technical Field
The invention relates to the technical field of chemical industry, in particular to an amphiphilic polymer with a comb-shaped structure, and a preparation method and application thereof.
Background
The lithium ion battery mainly comprises a positive electrode, a negative electrode, a diaphragm and electrolyte. The positive electrode and the negative electrode are formed by mixing an active material, a conductive agent, a binder, and the like into a slurry, and then coating the slurry on a current collector. The negative electrode active material is usually a carbon material. The positive electrode active material is usually a lithium-containing compound, and the positive electrode active materials which are commercially applied on a large scale at present mainly comprise several types of lithium iron phosphate, lithium manganese iron phosphate, lithium manganate, ternary materials of lithium nickel cobalt manganate and lithium nickel cobalt aluminate. The lithium iron phosphate as the positive electrode has the characteristics of low cost, high safety and long cycle life, and is increasingly valued and applied on a large scale; lithium iron phosphate has been regarded as having a higher voltage plateau and energy density than lithium iron phosphate.
The lithium iron phosphate (LFP) and lithium manganese iron phosphate (LMFP) which are commercially used at present are basically obtained by jet milling spherical LFP and LMFP, the particle size of the nano-structure material is about 100-500 nm, and compared with the bulk and micron-sized electrode materials, the nano-structure material has the advantages of short transmission distance, large specific surface area, high reversible capacity, stable cycle performance, higher electron transmission speed and the like. Although nanoscale particles have a stronger electrolyte adsorption capacity than micron-sized particles, their surface energy due to their large specific surface area also makes them very susceptible to agglomeration. Meanwhile, the conductive agent also has larger specific surface area, is difficult to be completely dispersed in the glue solution, and brings inconvenience to processing. In the pulping process, the agglomeration and agglomeration cause uneven slurry dispersion, and the conductive agent cannot uniformly cover the active material, so that the conductivity of the positive electrode is reduced, and the capacity, the cycle performance and the consistency of the lithium ion battery are directly reduced. The agglomeration causes the adhesion of the slurry to be reduced during the coating process, increases the internal resistance of the battery, and the protruding portion is easily pressed to pierce the separator during the assembly process, thereby reducing the safety of the battery.
The solid content of the lithium iron (manganese) phosphate anode slurry used in the anode preparation process is usually 50-55wt%, when the solid content of the slurry is continuously improved, the viscosity of the slurry is greatly increased, the viscosity change in the storage process is large, the fluidity of the slurry is reduced, the construction difficulty is increased, and the electrical performance is reduced. The surfactant (dispersing agent comprising anionic surfactant and nonionic surfactant) is added into the lithium iron (manganese) phosphate slurry to disperse the small particles, so that the performance of the slurry is improved, and the small particles are prevented from agglomerating. However, the addition of the conventional dispersing agent generally has adverse effects on the performance of the battery, for example, the addition of the anionic surfactant only can generate salting-out effect, so that the peeling strength of the electrode is obviously reduced, and the stability of the slurry is poor; only adding nonionic surfactant can form micelle, which affects mobility of electrons and has poor conductivity of positive electrode.
At present, high molecular weight polyvinylpyrrolidone is generally used as a dispersing agent in industry to prepare corresponding dispersing liquid, but the dispersing efficiency of the dispersing agent is low, and the viscosity of a dispersing liquid product is high, so that the conductivity is poor. In order to reduce the viscosity of the anode material of the lithium iron (manganese) phosphate battery in the homogenization process, the solid content of the slurry has to be reduced by increasing the solvent consumption to meet the quality requirement of the product. Therefore, how to increase the solid content of the lithium (manganese) iron phosphate cathode slurry, reduce the viscosity of the slurry and maintain the fluidity and stability of the slurry is a great problem at present, and therefore, there is room for improvement.
Disclosure of Invention
In order to solve the problems mentioned in the background art, the present invention provides an amphiphilic polymer with a comb structure, which is prepared by copolymerizing a single-end vinyl polyether monomer, a vinyl monomer with an acid group, other vinyl monomers and a (meth) acrylamide monomer with a long-chain alkyl structure in a random free radical solution under the action of an initiator, wherein the corresponding structural formula is as follows:
wherein a, b, c, d is natural positive integer, R 1 is-H or-COOH, R 2 is-H or-CH 3 ,R 3 Is single-end amino polyether radical, R 4 Is phenyl, pyridyl or pyrrolidinonyl, R 5 Is long chain alkyl amino.
Preferably, the single-ended vinyl polyether monomer is synthesized by organic reaction of single-ended amine polyether and vinyl-containing anhydride in the presence of a polymerization inhibitor, wherein the vinyl-containing anhydride is selected from any one of methacrylic anhydride, acrylic anhydride and maleic anhydride.
Preferably, the vinyl monomer of the acidic group is selected from any one of acrylic acid, methacrylic acid, itaconic acid, vinyl phosphonic acid, 2-hydroxyethyl methacrylate phosphate.
Preferably, the other vinyl monomer is selected from any one of styrene, vinyl pyridine and N-vinyl pyrrolidone.
Preferably, the (meth) acrylamide monomer having a long chain alkyl structure is selected from any one of N-dodecyl acrylamide, N-hexadecyl acrylamide, N-octadecyl acrylamide, N-dodecyl methacrylamide, N-hexadecyl methacrylamide and N-octadecyl methacrylamide.
Preferably, the solvent used in the random radical solution copolymerization is selected from any one of methanol, ethanol, isopropanol, N-methylpyrrolidone, ethylene glycol butyl ether, diethylene glycol butyl ether, ethylene glycol methyl ether, diethylene glycol methyl ether, propylene glycol methyl ether, dipropylene glycol methyl ether, propylene glycol butyl ether, dipropylene glycol butyl ether, PPG200, PEG200, N-dimethylformamide and dimethyl sulfoxide.
Preferably, the initiator is azo initiator or peroxy compound initiator;
the azo initiator is selected from any one of azodiisobutyronitrile and azodiisoheptonitrile;
the peroxide compound initiator is selected from any one of benzoyl peroxide, lauroyl peroxide, tert-butyl peroxybenzoate, tert-butyl peroxyvalerate, cumene hydroperoxide, tert-butyl hydroperoxide, dicumyl peroxide, di-tert-butyl peroxide and di-tert-amyl peroxide.
Preferably, if the total mass of the polymerized monomers is 100 parts, the amount of the single-ended vinyl polyether monomer is 1 to 30 parts, the amount of the vinyl monomer having an acidic group is 1 to 20 parts, the amount of the other vinyl monomer is 1 to 70 parts, and the amount of the (meth) acrylamide monomer having a long chain alkyl structure is 1 to 50 parts.
The invention also provides a preparation method of the amphiphilic polymer, which comprises the following steps:
s1, preparing materials dropwise added in batches
The materials comprise a solution A and a solution B;
the solution A consists of all monomers, part of initiator and part of solvent;
the solution B consists of the rest of the initiator and the rest of the solvent;
s2, carrying out polymerization reaction
Adding part of solvent into a reaction bottle, heating and refluxing for 30-60min, dripping solution A for 1-3h, refluxing for 2-3h after dripping, dripping half of solution B for 1-2h after dripping, continuously dripping the rest of solution B, refluxing for 2-5h after dripping, and removing the low boiling point solvent to obtain the amphiphilic polymer solution.
The invention also provides application of the amphiphilic polymer serving as a dispersing agent in the anode material of the lithium iron phosphate (manganese) battery.
Compared with the prior art, the invention has the beneficial effects that:
1. the macromolecular main chain of the amphiphilic polymer synthesized by the invention has strong polar groups carboxyl or phosphate (phosphonic) groups which can be adsorbed on the surfaces of carbon nano-tube particles, lithium iron phosphate particles and acetylene black particles, and the side chains are long-chain alkyl groups and polyether groups which have good compatibility with methyl pyrrolidone solvent, so that the inorganic particles with the corresponding particles adsorbed with the dispersing agent on the surfaces can be well dispersed in the methyl pyrrolidone solvent through the steric hindrance effect, and the mutual collision among the particles caused by Brownian motion is prevented, and the aggregation and agglomeration among the particles are caused. Therefore, the dispersing agent of the amphiphilic comb polymer can achieve the purposes that particles are easy to disperse and the formed dispersing liquid has good dispersion stability.
2. The amphiphilic polymer developed by the invention is used as a dispersing agent, has the effects of good viscosity reduction and high dispersing efficiency in the homogenization of the anode material of the lithium iron (manganese) phosphate battery, and can effectively maintain the stability of the dispersing liquid, thereby greatly reducing the production cost and achieving the purposes of energy conservation and environmental protection.
Drawings
FIG. 1 is an infrared plot of the polymer obtained in example 1;
FIG. 2 is an infrared plot of the polymer obtained in example 2;
FIG. 3 is an infrared plot of the polymer obtained in example 3.
Detailed Description
Raw materials are commercially available for use in the present invention unless otherwise specified.
Preparation example 1
Synthesis of monomer mixtures with single-ended vinyl polyethers and methacrylic acid
200g of single-ended amine polyether M2070 and 0.07 g of polymerization inhibitor para-hydroxyanisole are added into a reaction bottle, and after being stirred uniformly, 15.4g of methacrylic anhydride is added dropwise under stirring at room temperature, the temperature is kept to be not more than 100 ℃, after the dropwise addition is completed, the reaction is continued for 1h at 100 ℃, and a mixture of single-ended vinyl polyether monomer and methacrylic acid monomer is obtained, and the mixture is refrigerated and stored at 4 ℃.
Preparation example 2
Synthesis of (meth) acrylamide monomer and methacrylic acid monomer mixture having long-chain alkyl structure
269.5g of octadecylamine, 0.16g of polymerization inhibitor p-hydroxyanisole and 106g of solvent N-methylpyrrolidone are added into a reaction bottle, after stirring and dissolving, 154g of methacrylic anhydride is dropwise added at room temperature under stirring, the temperature is kept at not more than 100 ℃, after the dropwise adding is completed, the reaction is continued for 1h at 100 ℃, and a mixture of (methyl) acrylamide monomer and methacrylic acid monomer with long-chain alkyl structure is obtained, and the mixture is refrigerated and stored at 4 ℃.
Example 1
S1, preparing materials dropwise added in batches
The materials comprise a solution A and a solution B;
the solution A consisted of 21.4g of the mixture of single-ended vinyl polyether monomer and methacrylic monomer obtained in preparation example 1, 11.2g of other vinyl monomers, 52.6g of the mixture of (meth) acrylamide monomer and methacrylic monomer having a long-chain alkyl structure obtained in preparation example 2, 90g of PEG200 and 0.3g of AIBN;
the solution B consists of 10g of isopropanol and 0.08g of AIBN;
s2, carrying out polymerization reaction
Adding 30g of isopropanol into a reaction bottle, heating and refluxing for 45 min, dropwise adding the solution A for 2h, carrying out reflux reaction for 2.5h after the completion of dropwise adding, then dropwise adding half of the solution B, carrying out reflux reaction for 1.5h after the completion of dropwise adding, continuing dropwise adding the rest of the solution B, carrying out reflux reaction for 3.5h after the completion of dropwise adding, and removing the low-boiling point solvent to obtain a solution consisting of the amphiphilic polymer and the PEG 200.
In this example, the vinyl monomer having an acidic group is methacrylic acid, and the other vinyl monomer is styrene.
Example 2
This embodiment differs from embodiment 1 in that: the other vinyl monomer was vinylpyridine and the amount added was 11.2g.
Example 3
S1, preparing materials dropwise added in batches
The materials comprise a solution A and a solution B;
the solution A consists of 21.4g of the mixture of single-ended vinyl polyether monomer and methacrylic acid monomer obtained in preparation example 1, 11.2g of other vinyl monomers, 52.6g of the mixture of (meth) acrylamide monomer with long-chain alkyl structure obtained in preparation example 2 and methacrylic acid monomer, 25g of ethylene glycol butyl ether, 25g of propylene glycol methyl ether and 1g of di-tert-amyl peroxide;
the solution B consists of 5g of ethylene glycol butyl ether, 5g of propylene glycol butyl ether and 0.4g of di-tert-amyl peroxide;
s2, carrying out polymerization reaction
Adding 15g of ethylene glycol butyl ether and 15g of propylene glycol methyl ether into a reaction bottle, heating and refluxing for 45 min, dripping solution A for 2h, refluxing for 2.5h after dripping, dripping half of solution B, refluxing for 1.5h after dripping, continuously dripping the rest of solution B, and refluxing for 3.5h after dripping to obtain a solution consisting of the amphiphilic polymer, the ethylene glycol butyl ether and the propylene glycol butyl ether.
In this example, the vinyl monomer having an acidic group is methacrylic acid, and the other vinyl monomer is N-vinylpyrrolidone.
In FIGS. 1-3, the wave number is 3410cm -1 To 3460cm -1 The range is the telescopic vibration absorption peak of carboxyl hydroxyl and the wave number is 1300cm -1 Is carboxyl hydroxyl deformation vibration absorption peak with wave number of 1665-1670 cm -1 Are carbonyl absorption peaks in carboxylic acids with hydrogen bond interactions, which indicate that carboxyl groups, which are acidic groups introduced by methacrylic monomer mer units through copolymerization, are present on the three macromolecular backbones. In the spectrogram, the wave number is 2922cm -1 The nearby strong absorption peaks are methyl and methine telescopic vibration absorption peaks with wave number of 1464cm -1 The absorption peaks are methyl and methine deformation vibration absorption peaks, and the wave number is 652cm -1 The left and right absorption peaks are long-chain alkyl- (CH) 2 ) n Typical backbone vibration absorption peak. These data indicate that long chain alkyl groups have been introduced into the polymer chain by copolymerization of N-octadecyl methacrylamide monomer with other monomers. In the three infrared spectrograms, the wave number is 1113-1117cm -1 The range has a strong absorption peak, which is typical of C-O-C bonds, indicating that polyether molecules have also been incorporated into the macromolecular chains of the present invention. The wavenumber present in FIG. 1 is 3036cm -1 A weak absorption peak, 1504cm -1 These are typical phenyl absorption peaks formed by the introduction of styrene monomer into the macromolecular chain at a strong absorption peak. Two typical absorption peaks are shown in FIG. 2 for the presence of pyridine ring groups in the molecular chain. One is that the CH stretching vibration absorption peak 3150cm in the five-membered ring is shown -1 ~3130cm -1 This is a weak shoulder and the other is at wave number 1464cm -1 Is a strong absorption peak of the five-membered ring. FIG. 3 shows that the typical infrared absorption peak showing the presence of pyrrolidone groups in the molecular chain has a wave number of 2954cm -1 CH telescopic vibration absorption peak in pyrrolidone ring of 1666cm -1 C=o stretching vibration absorption peak in pyrrolidone ring and 1300cm -1 C-N stretching vibration absorption peak of (C-N).
Lithium iron phosphate anode material battery homogenizing result and detection
Firstly, dispersing 2.3 parts by mass of PVDF and 60 parts by mass of NMP to prepare PVDF solution, then adding 0.22 part by mass of polymer samples obtained in examples 1-3 or polyvinylpyrrolidone (average molecular weight 58000) serving as a comparative example to uniformly disperse, continuously adding 95.9 parts by mass of lithium iron phosphate and 1 part by mass of acetylene black, using zirconium beads of 2-3mm, vibrating and grinding for 1h according to the weight ratio of the dispersion liquid to the zirconium beads of 1:1, adding 0.8 part by mass of carbon nano tube slurry to uniformly disperse, and testing fineness by a fineness meter and viscosity by a rotational viscosimeter. The dispersion was knife coated onto a PET film using a 100 μm bar, dried in an oven at 110 ℃ for 40 minutes to form a film, and the resistance of the film was measured using a four-probe tester. The results are shown in Table 1.
TABLE 1
Lithium manganese iron phosphate anode material battery homogenizing result and detection
Firstly, preparing PVDF solution by dispersing 2.35 parts by mass of PVDF and 34.5 parts by mass of NMP at high speed; then, 0.53 parts by mass of the polymer sample obtained in example 1-3 or comparative polyvinylpyrrolidone (average molecular weight 58000) was added to 6.49 parts by mass of NMP and dispersed uniformly, then 55 parts by mass of lithium iron manganese phosphate and 0.63 parts by mass of SP conductive carbon black were added together, zirconium beads of 2-3mm were used, and after shaking and grinding for 1 hour in a weight ratio of 1:1 of dispersion to zirconium beads, 0.5 parts by mass of carbon nanotube slurry was added and dispersed uniformly, and the fineness and rotational viscosimeter were used to test the viscosity, respectively. The dispersion was knife coated onto a PET film using a 100 μm bar, dried in an oven at 110 ℃ for 40 minutes to form a film, and the resistance of the film was measured using a four-probe tester. The results are shown in Table 1.
TABLE 2
The foregoing is only a preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art, who is within the scope of the present invention, should make equivalent substitutions or modifications according to the technical scheme of the present invention and the inventive concept thereof, and should be covered by the scope of the present invention.

Claims (10)

1. The amphiphilic polymer with comb structure is characterized in that the polymer is prepared by random free radical solution copolymerization of single-ended vinyl polyether monomer, vinyl monomer with acid group, other vinyl monomer and (methyl) acrylamide monomer with long-chain alkyl structure under the action of initiator, and the corresponding structural formula is shown as follows:
wherein a, b, c, d is natural positive integer, R 1 is-H or-COOH, R 2 is-H or-CH 3 ,R 3 Is single-end amino polyether radical, R 4 Is phenyl, pyridyl or pyrrolidinonyl, R 5 Is long chain alkyl amino.
2. The amphiphilic polymer with comb structure according to claim 1, wherein the single-ended vinyl polyether monomer is synthesized by organic reaction of single-ended amine polyether and vinyl-containing anhydride in the presence of polymerization inhibitor, wherein the vinyl-containing anhydride is selected from any one of methacrylic anhydride, acrylic anhydride and maleic anhydride.
3. An amphiphilic polymer having a comb structure according to claim 1, wherein the vinyl monomer of the acidic group is selected from any one of acrylic acid, methacrylic acid, itaconic acid, vinyl phosphonic acid, 2-hydroxyethyl methacrylate phosphate.
4. An amphiphilic polymer having a comb structure according to claim 1, wherein the other vinyl monomer is selected from any one of styrene, vinyl pyridine, N-vinyl pyrrolidone.
5. An amphiphilic polymer having a comb structure according to claim 1, wherein the (meth) acrylamide monomer of long chain alkyl structure is selected from any one of N-dodecyl acrylamide, N-hexadecyl acrylamide, N-octadecyl acrylamide, N-dodecyl methacrylamide, N-hexadecyl methacrylamide, N-octadecyl methacrylamide.
6. The comb-structured amphiphilic polymer according to claim 1, wherein the solvent used in the random radical solution copolymerization is selected from any one of methanol, ethanol, isopropanol, N-methylpyrrolidone, ethylene glycol butyl ether, diethylene glycol butyl ether, ethylene glycol methyl ether, diethylene glycol methyl ether, propylene glycol methyl ether, dipropylene glycol methyl ether, propylene glycol butyl ether, dipropylene glycol butyl ether, PPG200, PEG200, N-dimethylformamide, and dimethyl sulfoxide.
7. An amphiphilic polymer having a comb structure according to claim 1, wherein the initiator is an azo-type initiator or a peroxy compound initiator;
the azo initiator is selected from any one of azodiisobutyronitrile and azodiisoheptonitrile;
the peroxide compound initiator is selected from any one of benzoyl peroxide, lauroyl peroxide, tert-butyl peroxybenzoate, tert-butyl peroxyvalerate, cumene hydroperoxide, tert-butyl hydroperoxide, dicumyl peroxide, di-tert-butyl peroxide and di-tert-amyl peroxide.
8. The amphiphilic polymer with comb structure according to claim 1, wherein the amount of single-ended vinyl polyether monomer is 1-30 parts, the amount of vinyl monomer with acid group is 1-20 parts, the amount of other vinyl monomer is 1-70 parts, and the amount of (meth) acrylamide monomer with long chain alkyl structure is 1-50 parts, if the total mass of the polymerized monomers is 100 parts.
9. A process for the preparation of an amphiphilic polymer according to any one of claims 1 to 8, comprising the steps of:
s1, preparing materials dropwise added in batches
The materials comprise a solution A and a solution B;
the solution A consists of all monomers, part of initiator and part of solvent;
the solution B consists of the rest of the initiator and the rest of the solvent;
s2, carrying out polymerization reaction
Adding part of solvent into a reaction bottle, heating and refluxing for 30-60min, dripping solution A for 1-3h, refluxing for 2-3h after dripping, dripping half of solution B for 1-2h after dripping, continuously dripping the rest of solution B for 2-5h after dripping, and removing the low boiling point solvent to obtain the amphiphilic polymer solution.
10. Use of an amphiphilic polymer according to any one of claims 1-8 as a dispersant in a (manganese) iron lithium phosphate battery positive electrode material in a homogenate.
CN202310628881.0A 2023-05-31 2023-05-31 Amphiphilic polymer with comb-shaped structure and preparation method and application thereof Pending CN116655859A (en)

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CN116082571A (en) * 2022-12-31 2023-05-09 上海宇昂水性新材料科技股份有限公司 PVP comb-type copolymer and preparation method and application thereof

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