CN108219164A - A kind of preparation method of heat-conducting polymer material - Google Patents

A kind of preparation method of heat-conducting polymer material Download PDF

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Publication number
CN108219164A
CN108219164A CN201711436267.5A CN201711436267A CN108219164A CN 108219164 A CN108219164 A CN 108219164A CN 201711436267 A CN201711436267 A CN 201711436267A CN 108219164 A CN108219164 A CN 108219164A
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high molecular
solvent
preparation
molecular material
heat
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杨晓锋
孔令学
游艳
伊智峰
顾海军
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Shanghai Xinyao Electronics Co Ltd
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Shanghai Xinyao Electronics Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/205Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase
    • C08J3/21Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase the polymer being premixed with a liquid phase
    • C08J3/212Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase the polymer being premixed with a liquid phase and solid additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2369/00Characterised by the use of polycarbonates; Derivatives of polycarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K7/00Use of ingredients characterised by shape
    • C08K7/22Expanded, porous or hollow particles
    • C08K7/24Expanded, porous or hollow particles inorganic

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The present invention provides a kind of preparation method of heat-conducting polymer material, and the preparation method includes at least following steps:1) high molecular material mixed liquor is formed after by high molecular material dissolving in a solvent, adding in heat filling mixing;2)High molecular material mixed liquor with flocculation solvent is mixed and obtains composite material master batch.The present invention can be effectively improved dispersibility of the heat filling in high molecular material intrinsic silicon by the method for solution blending, so that the thermal conducting path that heat filling is formed in the base can reach another surface from a surface, and the uneven caused heat aggregation of filler distribution is not had.

Description

A kind of preparation method of heat-conducting polymer material
Technical field
The present invention relates to a kind of high molecular material, more particularly to a kind of preparation method of heat-conducting polymer material.
Background technology
High molecular material compared with metal and inorganic non-metallic material have low processing cost, it is light-weight, easily molded, can return Receipts, excellent mechanical property are suitable for the characteristics such as range is wide.It is daily with the people that high molecular material has become the development of the national economy It lives essential important materials.But high molecular material free electron limitation of movement system and be generally believed that be it is hot absolutely Edge body, thermal conductivity factor usually in 0.3W/mK hereinafter, which greatly limits high molecular material heat dissipation and Heat Conduction Material field should With.Therefore, under the premise of high molecular material primary characteristic is ensured, assigning high molecular material heat conductivility can greatly extend The application range of high molecular material, and be also a very big challenge.
At present, one of method for preparing heat-conducting polymer material is to use high molecular material in itself as raw material, accurate Under conditions of control heating and stretching, the strand of the high molecular material of ultra high molecular weight is made to be arranged in same direction.Although High molecular material obtained has very high thermal conductivity factor (104W/ on the direction arranged along strand in this way MK), but for the rigors of condition control and the selection of raw material, it is not appropriate for producing on a large scale.
In traditional polymer composite production technology, extruding pelletization process is essential.This physics is total to The defects of mixed method easily causes filler to assemble in high molecular material matrix, formation interiors of products and surface, so as to generation Performance impacts.
Invention content
In view of the foregoing deficiencies of prior art, the purpose of the present invention is to provide a kind of heat-conducting polymer material, It is directly granulated based on solwution method, replaces the production technology of traditional extruding pelletization, for solving macromolecule in the prior art The problem of thermal conductivity of material is poor, and processing is not easy and high molecular material mixes uneven the defects of causing.
In order to achieve the above objects and other related objects, the present invention is what is realized by including following technical solution.
The present invention provides a kind of preparation method of heat-conducting polymer material, and the preparation method includes the following steps:
1) high molecular material mixed liquor is formed after by high molecular material dissolving in a solvent, adding in heat filling mixing;
2) high molecular material mixed liquor with flocculation solvent is mixed and obtains composite material master batch.
Then, can the composite material master batch of acquisition be squeezed out to injection molding or coating forms a film.
Preferably, the high molecular material is selected from makrolon (PC), acrylonitrile-butadiene-styrene (ABS) (ABS), poly- first It is one or more in base methyl acrylate (PMMA), polyetherimide (PEI), polystyrene (PS) and polyvinyl alcohol (PVA). It is highly preferred that the high molecular material is makrolon.It is highly preferred that the makrolon is bisphenol-a polycarbonate.
Preferably, the heat filling is selected from expanded graphite, carbon nanotube, boron nitride, aluminium oxide, aluminium nitride, carbonization One or more of silicon, metallic particles or metal nanometer line are compound.It is highly preferred that the carbon nanotube includes single Pipe and multi-arm carbon nano-tube.It is highly preferred that metal in the metallic particles or metal nanometer line in silver, gold and copper one Kind is a variety of.
It is highly preferred that the heat filling is expanded graphite.
Preferably, it is counted on the basis of gross mass of the expanded graphite with the high molecular material, the heat filling Mass percentage is 1~5wt%.
As expanded graphite, refer to that a variety of chemical substances such as acid, alkali metal, salt are inserted between graphite laminate structure, institute The compound between graphite layers (also may be referred to expansible graphite) of formation, then it is made to expand obtained substance by high temperature.Make stone The method of black intercalation compound expansion has high-temperature heating, flame calcination and microwave radiation.Volume after it is expanded can reach Hundred times before, so as to form similar vermiform structure.Expanded graphite used in the present invention preferably passes through microwave spoke Compound between graphite layers after penetrating, preferably 600 μm of size, the preferred 3-7mm of length.
Preferably, when high molecular material is makrolon, the solvent is 1,3-dioxolane;When high molecular material is During ABS, the solvent is dichloromethane;When high molecular material is polyetherimide, the solvent is N- methyl -2- pyrrolidines Ketone;When high molecular material is polymethyl methacrylate, the solvent is acetone;When high molecular material is polystyrene, The solvent is toluene;When high molecular material is polyvinyl alcohol, the solvent is acetic acid.
Preferably, the flocculation solvent is water or organic solvent.
It is highly preferred that when using water as flocculation solvent, surfactant is added in water to reduce water surface tension. The surfactant appointing in anion surfactant, cationic surfactant and nonionic surfactant It is a kind of.
Preferably, the anion surfactant includes grade fatty acid salt, and aliphatic hydrocarbon is generally the length of 11-17 carbon Chain;Hydrosulphate, fat hydrocarbon chain is between 12-18 carbon;Azochlorosulfonate acid compound, fat hydrocarbon chain is between 8-18 carbon.
Preferably, the cationic surfactant includes amine salt, quaternary ammonium salt, heterocyclic, hello salt form, fat Fat hydrocarbon chain is between 8-18 carbon.
Preferably, the nonionic surfactant include alkyl phenol polyoxyethylene ether, high-carbon fatty alcohol polyoxyethylene ether, Polyoxyethylene carboxylate, fatty acid methyl ester ethoxylate, polypropylene glycol ethylene oxide adduct, it is polyoxyethylated from Subtype surfactant, sorbitan ester, sucrose ester and alkylolamides type.
It is highly preferred that the organic solvent is selected from arene, fat hydrocarbon, alicyclic hydrocarbon type, chlorinated hydrocarbons, alcohols, ether It is one or more in class, esters, ketone, alcohol derivatives, acetonitrile, pyridine and phenol.It is highly preferred that the flocculation solvent choosing From one or more in water, ethyl alcohol and ethylene glycol.
Preferably, the arene includes one or more in benzene, toluene and dimethylbenzene.
Preferably, the alicyclic hydrocarbon type includes one or more in hexamethylene, cyclohexanone and toluene cyclohexanone.
Preferably, the fat hydrocarbon includes one or more in pentane, hexane and octane.
Preferably, the chlorinated hydrocarbons include one or more in chlorobenzene, dichloro-benzenes, dichloromethane and chloroform.
Preferably, the alcohols includes one kind or more in methanol, ethyl alcohol, normal propyl alcohol, isopropanol, ethylene glycol and glycerine Kind.
Preferably, the ethers includes one or more in ether and propylene oxide.
Preferably, the esters include one or more in methyl acetate, ethyl acetate and propyl acetate.
Preferably, the ketone includes one or more in acetone, espeleton and methylisobutylketone.
Preferably, the alcohol derivatives are included in glycol monoethyl ether, ethylene glycol monoethyl ether and ethylene glycol monobutyl ether It is one or more.
Preferably, mixed method described in step 1) is mixed including ultrasonic disperse, mechanical agitation, magnetic agitation or mixer It closes.It is highly preferred that mixed method described in step 1) is ultrasonic disperse mixing and magnetic agitation mixing.
Preferably, the composite material master batch obtained in step 2) is 0.005~5mm.
As described above, the preparation method of the heat-conducting polymer material of the present invention, has the advantages that:
The present invention can be effectively improved point of the heat filling in high molecular material intrinsic silicon by the method for solution blending Property is dissipated, so that the thermal conducting path that heat filling is formed in the base can reach another surface from a surface, and The uneven caused heat aggregation of filler distribution is not had.Polymer composite mixed liquor after solvent blending can directly be made Grain and obtain polymer composite master batch.
Description of the drawings
Fig. 1 is the process schematic of the stirring-granulating in the embodiment of the present application.
Fig. 2 is the process schematic of the fluidized granulation in the embodiment of the present application.
Specific embodiment
Before further describing the specific embodiments of the present invention, it should be appreciated that protection scope of the present invention is not limited to down State specific specific embodiment;It is also understood that the term used in the embodiment of the present invention is specific specific in order to describe Embodiment, the protection domain being not intended to be limiting of the invention.The test method of actual conditions is not specified in the following example, Usually according to normal condition or the condition proposed by according to each manufacturer.
When embodiment provides numberical range, it should be appreciated that except non-present invention is otherwise noted, two ends of each numberical range Any one numerical value can be selected between point and two endpoints.Unless otherwise defined, in the present invention all technologies for using and Scientific terminology is identical with the normally understood meaning of those skilled in the art of the present technique.Except used in embodiment specific method, equipment, Outside material, according to record of the those skilled in the art to the grasp of the prior art and the present invention, it can also use and this Any method, equipment and the material of the similar or equivalent prior art of method, equipment described in inventive embodiments, material come real The existing present invention.
【High molecular material】
As the high molecular material being used as in the present invention, it is not limited to cited material in the present invention.As long as it looks for To the corresponding solvent of high molecular material, it is possible to prepare polymer composite by the method in the present invention.In the present invention Method has polymeric material field fairly good applicability.
Preferably PC of the invention is as high molecular material, more preferably bisphenol-a polycarbonate (Sabic Products Lexan141R).As the preferred dioxolanes of solvent of dissolving PC, purity>99%.PC used in the present invention is in dioxolanes In concentration highest can reach 15wt%, after this concentration, formation gels of the PC in dioxolanes.In addition, dioxy The purity of penta ring need to ensure more than 99% that the dioxolanes of low-purity is insufficient simultaneously for the PC dissolvings used in the present invention It is precipitated with the presence of white granular.
【Heat filling】
As the preferred expanded graphite of heat filling being used as in the present invention.
As expanded graphite, refer to that a variety of chemical substances such as acid, alkali metal, salt are inserted between graphite laminate structure, institute The compound between graphite layers (also may be referred to expansible graphite) of formation, then it is made to expand obtained substance by high temperature.Make stone The method of black intercalation compound expansion has high-temperature heating, flame calcination and microwave radiation.Volume after it is expanded can reach Hundred times before, so as to form similar vermiform structure.Expanded graphite used in the present invention preferably passes through microwave spoke Compound between graphite layers after penetrating, preferably 600 μm of size, the preferred 3-7mm of length.
【Flocculate solvent】
As flocculation solvent, the foundation selected is can dissolve each other, and cannot dissolve height with dissolving the solvent of high molecular material Molecular material.PC and its solvent butyl oxide link used in the present invention, the optional water of flocculation solvent, methanol, ethyl alcohol, acetone, second two Alcohol etc., preferably water, ethylene glycol.
Water,, will not when being directly added into polymer composite mixed liquor since its surface tension is very big as flocculation solvent Spheric granules is formed, and film is formed on the surface of water, therefore, it is necessary to add in surfactant in water to reduce its surface Power.As surfactant, (including higher fatty acid salt, aliphatic hydrocarbon is generally 11-17 carbon to optional anion surfactant Long-chain;Hydrosulphate, fat hydrocarbon chain is between 12-18 carbon;Azochlorosulfonate acid compound, fat hydrocarbon chain is between 8-18 carbon), sun from Sub- surfactant (including amine salt, quaternary ammonium salt, heterocyclic, hello salt form, fat hydrocarbon chain is between 8-18 carbon) and Nonionic surfactant (including alkyl phenol polyoxyethylene ether, high-carbon fatty alcohol polyoxyethylene ether, polyoxyethylene carboxylate, Fatty acid methyl ester ethoxylate, polyoxyethylated ionic surfactant, loses the ethylene oxide adduct of polypropylene glycol Water sorbitol ester, sucrose ester, alkylolamides type) it is any.For different types of surfactant, in water dense As long as degree is more than when critical micelle concentration can avoid adding in polymer composite mixed liquor forms film on surface.
Organic solvent is as flocculation solvent, since its surface tension is respectively less than water, do not need to add in other additives and can To form polymer composite master batch.In addition, that there is a big difference is molten for the boiling point of selection and the solvent of dissolving high molecular material Agent can improve the organic efficiency of the solvent of next step to the greatest extent as flocculation solvent.For example, selection dioxolanes dissolving PC can select ethylene glycol as flocculation solvent.Wherein, the boiling point of dioxolanes is 75 DEG C, and the boiling point of ethylene glycol is 197.3 DEG C, using distillation more satisfactory recycling purity is can be obtained by when detaching both solvents.
【Prilling process】
The present invention proposes a kind of new prilling process for being directed to thermoplastic engineering plastic, passes through the method for solution blending Obtained polymer composite mixed liquor can directly obtain polymer composite master batch by way of stirring or flowing, So as to eliminate traditional extruding pelletization process.Prilling process proposed by the present invention greatly reduces thermal energy in conventional method Loss, and by that recycling design can be reused to greatest extent for the selection for the solvent that flocculates, this can be also reduced due to molten Cost caused by the use of agent.
As the process by stirring-granulating, as shown in Figure 1.Obtained polymer composite mixed liquor is added drop-wise to wadding In solidifying solvent, by stir flocculation solvent can the particle of polymer composite mixed liquor do not flock together and formed Polymer composite master batch.Used agitating mode can be mechanical agitation or magnetic agitation.In addition, it is flocculated by heating Solvent can cause master batch more quickly to solidify.It again can be by polymer composite master batch and mixed solvent point by filtering From.
As the process by fluidized granulation, as shown in Figure 2.Polymer composite mixed liquor is added drop-wise in flowing It flocculates in solvent, the flocculation solvent of flowing can prevent adjacent polymer composite master batch adhesion from luming, molten with flocculating Agent flow on filter screen to collect composite masterbatch, and mixed solvent can be collected in container.
Most polymer composite master batch obtains the master batch that can be molded by drying at last.
Embodiment
Hereinafter, list embodiment and comparative example is specifically explained the present invention, but the present invention is never by these examples Limitation.
Embodiment 1
1st, makrolon grain (accounting for 99wt% in the composite) is added in dioxolanes under stiring until completely molten Solution, obtained a concentration of 15wt%.
2nd, expanded graphite (1wt%) is added in the polycarbonate solution obtained by " 1 ", obtains composite material mixing Liquid.By mixed solution ultrasound or stirring 2 hours or until being uniformly dispersed.
3rd, water is added to immediately in good composite material solution mixed above, and vibrating allows PC equal with expanded graphite Even precipitation.Sample after precipitation is put into 60 DEG C of drying in baking oven, then prepares the sample of Hong Ganhou by holding the method for pressure Polymer composite material board.
Embodiment 2
The preparation method is the same as that of Example 1, and wherein PC accounts for 95wt% in the composite, and expanded graphite accounts for 5wt%.
Embodiment 3
The preparation method is the same as that of Example 1, and wherein PC accounts for 90wt% in the composite, and expanded graphite accounts for 10wt%.
【Performance characterization】
Polymer composite material board, various experimental results and performance evaluation such as 1 institute of table are obtained according to above-mentioned preparation method Show.Wherein, the glass transition temperature of the composite material after addition expanded graphite does not have significant impact.By to heat conduction system Several measure, more than 5 times of former PC matrixes thermal conductivity factor can be reached by adding in graphite, graphene or expanded graphite, highest, it was demonstrated that institute The heat conductivility for obtaining composite material increases significantly.
Table 1
The above, only presently preferred embodiments of the present invention, not to the present invention in any form with substantial limitation, It should be pointed out that for those skilled in the art, under the premise of the method for the present invention is not departed from, can also make Several improvement and supplement, these are improved and supplement also should be regarded as protection scope of the present invention.All those skilled in the art, Without departing from the spirit and scope of the present invention, when made using disclosed above technology contents it is a little more Dynamic, modification and the equivalent variations developed, are the equivalent embodiment of the present invention;Meanwhile all substantial technologicals pair according to the present invention The variation, modification and evolution of any equivalent variations that above-described embodiment is made still fall within the range of technical scheme of the present invention It is interior.

Claims (10)

1. a kind of preparation method of heat-conducting polymer material, which is characterized in that the preparation method includes at least following steps:
1) high molecular material mixed liquor is formed after by high molecular material dissolving in a solvent, adding in heat filling mixing;
2) high molecular material mixed liquor with flocculation solvent is mixed and obtains composite material master batch.
2. preparation method according to claim 1, which is characterized in that the high molecular material is selected from makrolon, propylene One kind or more in nitrile-butadiene-styrene, polyetherimide, polymethyl methacrylate, polystyrene and polyvinyl alcohol Kind.
3. preparation method according to claim 1, it is characterised in that:The heat filling is receives selected from expanded graphite, carbon One or more of mitron, boron nitride, aluminium oxide, aluminium nitride, silicon carbide, metallic particles or metal nanometer line are compound.
4. preparation method according to claim 2, which is characterized in that described molten when high molecular material is makrolon Agent is 1,3- dioxolanes;When high molecular material is acrylonitrile-butadiene-styrene (ABS), the solvent is dichloromethane;Work as height When molecular material is polyetherimide, the solvent is n-methyl-2-pyrrolidone;When high molecular material is polymethylacrylic acid During methyl esters, the solvent is acetone;When high molecular material is polystyrene, the solvent is toluene;When high molecular material is During polyvinyl alcohol, the solvent is acetic acid.
5. preparation method according to claim 1, which is characterized in that the flocculation solvent is water or organic solvent.
6. preparation method according to claim 5, which is characterized in that when using water as flocculation solvent, add in water Enter surfactant to reduce water surface tension.
7. preparation method according to claim 1, which is characterized in that the organic solvent is selected from arene, aliphatic hydrocarbon One kind in class, alicyclic hydrocarbon type, chlorinated hydrocarbons, alcohols, ethers, esters, ketone, alcohol derivatives, acetonitrile, pyridine and phenol or It is a variety of.
8. preparation method according to claim 7, which is characterized in that including one or more in following feature:
The arene includes one or more in benzene, toluene and dimethylbenzene;
The alicyclic hydrocarbon type includes one or more in hexamethylene, cyclohexanone and toluene cyclohexanone;
The fat hydrocarbon includes one or more in pentane, hexane and octane;
The chlorinated hydrocarbons include one or more in chlorobenzene, dichloro-benzenes, dichloromethane and chloroform;
The alcohols includes one or more in methanol, ethyl alcohol, normal propyl alcohol, isopropanol, ethylene glycol and glycerine;
The ethers includes one or more in ether and propylene oxide;
The esters include one or more in methyl acetate, ethyl acetate and propyl acetate;
The ketone includes one or more in acetone, espeleton and methylisobutylketone;
The alcohol derivatives include one or more in glycol monoethyl ether, ethylene glycol monoethyl ether and ethylene glycol monobutyl ether.
9. preparation method according to claim 1, which is characterized in that mixed method described in step 1) includes ultrasound point It dissipates, mechanical agitation, magnetic agitation or mixer mix.
10. preparation method according to claim 1, which is characterized in that the composite material master batch of acquisition is in step 2) 0.005~5mm.
CN201711436267.5A 2017-12-26 2017-12-26 A kind of preparation method of heat-conducting polymer material Pending CN108219164A (en)

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Cited By (1)

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CN110698838A (en) * 2019-10-30 2020-01-17 濮阳市盛通聚源新材料有限公司 Flexible conductive film based on polycarbonate and preparation method thereof

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CN110698838A (en) * 2019-10-30 2020-01-17 濮阳市盛通聚源新材料有限公司 Flexible conductive film based on polycarbonate and preparation method thereof
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