CN102633936B - Heat-swellable thermoplastic microspheres - Google Patents

Heat-swellable thermoplastic microspheres Download PDF

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CN102633936B
CN102633936B CN201210109302.3A CN201210109302A CN102633936B CN 102633936 B CN102633936 B CN 102633936B CN 201210109302 A CN201210109302 A CN 201210109302A CN 102633936 B CN102633936 B CN 102633936B
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heat
monomer
thermoplastic microspheres
swellable thermoplastic
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CN102633936A (en
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孙伟贤
刘峰
陈宝生
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XINENG CHEMICAL TECHNOLOGY (SHANGHAI) Co Ltd
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XINENG CHEMICAL TECHNOLOGY (SHANGHAI) Co Ltd
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Abstract

The present invention relates to a kind of heat-swellable thermoplastic microspheres, it mainly can be gathered monomer by olefinic and expandable substance obtains through suspension polymerisation, obtained heat-swellable thermoplastic microspheres be with thermoplastic polymer for shell and be core with expandable substance the microsphere with nucleocapsid structure, it is characterized in that, wherein said olefinic can gather monomer by acrylonitrile, acrylic ester monomer, acrylamide monomers, acrylate containing fluorine monomer and acrylic monomer composition, the gross weight of monomer can be gathered for 100wt% for calculating benchmark with described olefinic, can gather in monomer at described olefinic, acrylonitrile accounts for 30wt%��90wt%, methacrylate-based monomer accounts for 5wt%��50wt%, acrylamide monomers accounts for 1wt%��20wt%, acrylate containing fluorine monomer accounts for 0.01wt%��1.0wt%, acrylic monomer accounts for 0wt%��40wt%. the T of heat-swellable thermoplastic microspheres provided by the invention starts to be 160 DEG C-200 DEG C.

Description

Heat-swellable thermoplastic microspheres
Technical field
The present invention relates to the thermoplastic microspheres of a kind of heat-swellable.
Background technology
The thermoplastic microspheres of heat-swellable is a kind of main by with thermoplastic polymer for shell and the microsphere with nucleocapsid structure that constituted for core with expandable substance. In this type of microsphere, expandable substance is usually the boiling point liquid not higher than the softening temperature of thermoplastic polymer (shell). Heat, described liquid evaporates and increases intrinsic pressure, and meanwhile, described thermoplastic polymer (shell) softens, thus causing that (temperature that microsphere starts when expanding is abbreviated as T to described microsphere expansionStart, and temperature when realizing maximum swelling is abbreviated as TMaximum)��
In some applications, user wishes that the thermoplastic microspheres of the heat-swellable that supplier provides has higher TStart(being typically in 160 DEG C-200 DEG C). But, existing, there is higher TStartHeat-swellable thermoplastic microspheres in, methacrylonitrile becomes the necessary component (methacrylonitrile complex manufacturing and expensive) constituting thermoplastic polymer (shell), when there is no methacrylonitrile, performance (the mainly T of the thermoplastic microspheres of the heat-swellable preparedStartAnd swelliong power) user still can not be made satisfied.
Therefore it provides a kind of without methacrylonitrile and there is higher TStartThe heat-swellable thermoplastic microspheres of (being typically in 160 DEG C-200 DEG C) and relatively highly expanded ability becomes the technical issues that need to address of the present invention.
Summary of the invention
It is an object of the invention to, it is provided that a kind of without methacrylonitrile and there is higher TStartThe heat-swellable thermoplastic microspheres of (being typically in 160 DEG C-200 DEG C) and relatively highly expanded ability.
Heat-swellable thermoplastic microspheres provided by the present invention, it mainly can be gathered monomer by olefinic and expandable substance obtains through suspension polymerisation, obtained heat-swellable thermoplastic microspheres be with thermoplastic polymer for shell and be core with expandable substance the microsphere with nucleocapsid structure, it is characterized in that, wherein said olefinic can gather monomer by acrylonitrile, acrylic ester monomer, acrylamide monomers, acrylate containing fluorine monomer and acrylic monomer composition, the gross weight of monomer can be gathered for 100wt% for calculating benchmark with described olefinic, can gather in monomer at described olefinic, acrylonitrile accounts for 30wt%��90wt%, methacrylate-based monomer accounts for 5wt%��50wt%, acrylamide monomers accounts for 1wt%��20wt%, acrylate containing fluorine monomer accounts for 0.01wt%��1.0wt%, acrylic monomer accounts for 0wt%��40wt% (preferred 1wt%��30wt%),
Wherein, described acrylic ester monomer is selected from: the mixture of one or two or more kinds (containing two kinds) in compound race described in Formulas I, described acrylamide monomers is selected from: the mixture of one or two or more kinds (containing two kinds) in compound race described in Formula II, described acrylate containing fluorine monomer is selected from: the mixture of one or two or more kinds (containing two kinds) in compound race described in formula III, and described acrylic monomer is acrylic acid or/and methacrylic acid;
In formula, R1For C1��C10Straight chain, side chain or cyclic alkyl, R2And R3It is respectively and independently selected from: H, C1��C6The C that straight or branched alkyl or hydroxyl replace1��C6One, R in straight or branched alkyl4For C1��C6Straight or branched containing fluoroalkyl, R5For H or methyl.
The present invention mainly substitutes methacrylonitrile (monomer) in prior art with acrylamide monomers and acrylate containing fluorine monomer, it is thus achieved that have higher TStartThe heat-swellable thermoplastic microspheres of (being typically in 160 DEG C-200 DEG C) and relatively highly expanded ability, reaches the present invention and expects purpose.
Detailed description of the invention
Prepare the thermoplastic microspheres of heat-swellable of the present invention, existing suspension polymerization can be adopted. In described suspension polymerization, expandable substance and the polymerizable compound including polymerisable monomer by continuous stirring or add dispersion stabilizer (such as magnesium hydroxide or silica sol etc.) and keep suspended state. Through suspension polymerisation, polymer can be formed spherical.
In the present invention, to initiator used in expandable substance used and suspension polymerisation and cross-linking agent and have no special requirements.
For the selection of expandable substance, as long as meeting the boiling point of the selected expandable substance softening temperature not higher than thermoplastic polymer (shell) prepared by the present invention. The present invention recommends C5��C12Aliphatic hydrocarbon compounds, preferred expandable substance is C5��C12Straight or branched saturated hydrocarbons compound, it is preferred that expandable substance be C5��C8Straight or branched saturated hydrocarbons compound.
For the selection of cross-linking agent, the cross-linking agent being suitable for the present invention is the compound containing one or two or more kinds (containing two kinds) bridging property official group, and concrete cross-linking agent is one or two or more kinds (containing two kinds) mixture in following compounds:
Divinylbenzene, ethylene glycol bisthioglycolate (methyl) acrylate, two (ethylene glycol) two (methyl) acrylate, triethylene glycol two (methyl) acrylate, propylene glycol two (methyl) acrylate, BDO two (methyl) acrylate, 1,6-hexanediol two (methyl) acrylate, glycerol two (methyl) acrylate, 1,3 butylene glycol two (methyl) acrylate, neopentyl glycol two (methyl) acrylate, decamethylene-glycol two (methyl) acrylate, tetramethylolmethane three (methyl) acrylate, tetramethylolmethane four (methyl) acrylate, dipentaerythritol six (methyl) acrylate, triallylformal t pi three (methyl) acrylate, allyl methacrylate, trimethylolpropane tris (methyl) acrylate, three butanediol two (methyl) acrylate, PEG#200 bis-(methyl) acrylate, PEG#400 bis-(methyl) acrylate, PEG#600 bis-(methyl) acrylate, 3 acrylic acid oxygen base diol mono-acrylate, three acyl group formals, triallyl isocyanate, Triallyl isocyanurate, divinyl ether, ethylene glycol divinyl ether, diethylene glycol divinyl ether, triethyleneglycol divinylether, or TEG divinyl ether etc.
The consumption of cross-linking agent is the 0.1wt%��10wt% being used for preparing the total monomer weight of thermoplastic polymer (shell), and its preferred consumption is the 0.1wt%��3wt% being used for preparing the total monomer weight of thermoplastic polymer (shell).
Selection for initiator, the initiator (such as organic peroxide or azo compound etc.) being currently used for radical polymerization is suitable for the present invention, and concrete initiator is one or two or more kinds (containing two kinds) mixture in following compounds:
Two (cetyl) peroxy dicarbonate, two (4-tert-butylcyclohexyl) peroxy dicarbonate, peroxidating two is sad, diphenyl peroxide formic acid, peroxidating tin dilaurate, peroxidating two capric acid, t-butyl peracetate ester, the tert-butyl group crosses laurate, tert butyl peroxy benzoate, t-butyl hydroperoxide, cumene hydroperoxide, ethyl cumene peroxide, diisopropyl hydroxydicarboxylic acid's ester, 2, 2 '-azo double, two ((2, 4-methyl pentane nitrile), 2, 2 '-azo double, two (isopropyl cyanide), 1, 1 '-azo double, two (hexamethylene-1-nitrile), dimethyl 2, 2,-azo double, two (2 Methylpropionic acid ester), or 2, 2 '-azo double, two [2-methyl-N-(2-ethoxy)-propionic acid amide .] etc.
Can determining according to the kind of initiator used as described suspension polymerization temperatures, the suspension polymerization temperatures that the present invention recommends is 40 DEG C��100 DEG C, it is preferred that suspension polymerization temperatures is 45 DEG C��90 DEG C, and preferred suspension polymerization temperatures is 50 DEG C��85 DEG C.
For polymerization initial stage pressure, it is preferable that gauge pressure is 0-5.0MPa, and then preferred 0.1-3.0MPa, it is particularly preferred to 0.2-2.0MPa.
Additionally, preferably make it carry out suspension polymerisation in the aqueous dispersion medium containing dispersion stabilizer and/or stably dispersing auxiliary agent in the present invention. For the consumption that makes of described aqueous dispersion medium, there is no particular limitation, relative to the polymerizable components (can gather monomer total amount) of 100 weight portions, it is preferred to use 100 weight portions are to the aqueous dispersion medium of 1000 weight portions.
Wherein said dispersion stabilizer, it is possible to be that silica sol, gel calcium carbonate, magnesium hydroxide, calcium phosphate, aluminium hydroxide, hydrated ferric oxide., calcium sulfate, sodium sulfate, calcium oxalate, calcium carbonate, brium carbonate, magnesium carbonate are or/and alumina sol etc. The consumption of dispersion stabilizer is preferably the 0.1wt%��20wt% of polymerizable components (can gather monomer total amount) gross weight.
Further, above-mentioned stably dispersing auxiliary agent is selected from: the stably dispersing auxiliary agent of the polymer electrolytes such as diethanolamine and the condensation product of aliphatic dicarboxylic acid, gelatin, polyvinylpyrrolidone, methylcellulose, poly(ethylene oxide), polyvinyl alcohol, the cationic surfactants such as alkyl trimethylammonium chloride or chlorination dialkyl dimethyl ammonium, the anion surfactants such as alkyl sodium sulfate, the various emulsifying agents such as zwitterionic surfactant such as alkyl dimethyl aminoacetic acid glycine betaine, alkyl dihydroxyethyl aminoacetic acid glycine betaine. The consumption of stably dispersing auxiliary agent is preferably the 0.001wt%��2.0wt% of polymerizable components (can gather monomer total amount) gross weight.
The pH of aqueous dispersion medium during polymerization suitably determines according to the kind of the dispersion stabilizer used. Such as, if dispersion stabilizer is selected from: metal Ca, Mg, Ba, Zn, the salt of Ni and Mn, oxide or hydroxide are (concrete such as calcium phosphate, calcium carbonate, magnesium hydroxide, magnesium oxide, barium sulfate, calcium oxalate, with one or two or more kinds (containing two kinds) mixture in the hydroxide of zinc, nickel or manganese), the then preferred 5-12 of pH value, more preferably 6-10; If dispersion stabilizer is selected from: the oxide of starch, methylcellulose, hydroxypropyl methyl cellulose, carboxyl methylcellulose, glue agar, silica sol, colloidal clays or aluminum or ferrum or hydroxide, the then preferred 1-6 of pH value, more preferably 3-5.
It addition, water solublity free radical inhibitor also can be contained in aqueous dispersion medium, to suppress the generation of the cohesion microsphere in polymerization. As water solublity free radical inhibitor, can be alkali metal nitrites (sodium nitrite and/or potassium nitrite etc.), bichromate (Ammonium bichromate. (two ammonium chromates), sodium dichromate (two sodium chromates) and/or potassium dichromate (two Neutral potassium chromates) etc.), stannous chloride, stannic chloride, ferrous chloride, iron chloride, ferrous sulfate, the free radical inhibitor such as water soluble ascorbic acid class and derivant thereof. In the stability water, it is preferable that alkali metal nitrites. Every 100 parts by weight polymerizable components (can gather monomer total amount), the consumption of water solublity free radical inhibitor is 0.0001-1 parts by weight, it is preferable that 0.0003-0.1 parts by weight.
In aqueous dispersion medium used by the present invention, also can contain electrolyte. For electrolyte, there is no particular limitation, as being selected from: lithium chloride, sodium chloride, potassium chloride, magnesium chloride, calcium chloride, sodium bicarbonate, lithium sulfate, sodium sulfate, potassium sulfate, magnesium sulfate, sulphuric acid are by one or two or more kinds (containing two kinds) such as, sodium carbonate or benzoic acids. Relative to the aqueous dispersion medium of 100 parts by weight, electrolytical consumption is advisable with 0.1-50 parts by weight.
The average diameter of thermo-expandable microspheres provided by the present invention is 5 ��m��100 ��m, it is preferred that average diameter is 10 ��m��100 ��m, it is preferred that average diameter 10 ��m��60 ��m.
Additionally, with the thermo-expandable microspheres gross weight that provides for 100wt% for calculating benchmark, expandable substance accounts for 5wt%��50wt%, it is preferred that content is 10wt%��50wt%, it is preferred that content be 10wt%��40wt%, the optimum content of expandable substance is 10wt%��35wt%.
In presently preferred technical scheme, R1For C1��C6Straight or branched alkyl, preferred R1For C1��C3Straight or branched alkyl, best R1For methyl.
In a further preferred technical solution of the present invention, R2And R3It is respectively and independently selected from: H, C1��C3The C that straight or branched alkyl or hydroxyl replace1��C3One, preferred R in straight or branched alkyl2And R3It is respectively and independently selected from: a kind of in H, methyl or methylol, compound shown in best Formula II is acrylamide, N hydroxymethyl acrylamide or N,N-DMAA.
In a further preferred technical solution of the present invention, R4For C2��C4Straight or branched containing fluoroalkyl, best R4For trifluoroethyl or hexafluoro butyl.
When the polymerisation is essentially complete, can obtaining the microsphere of water paste or dispersion, they can be used as is or obtain so-called wet cake by any conventional method (such as bed filter, filter pressing, leaf filter, turn filter, band are filtered or are centrifuged and carry out dehydration). But, it is possible to by any conventional method (such as spray drying, support dry, tunnel drying, Rotary drying, drum dried, aeration-drying, turbo shelf dry, disk dries or fluid bed drying etc.), this microsphere is dried.
Outer surface at heat-swellable microsphere provided by the present invention also can attaching surface modifying agent, it is achieved dispersibility improve further or mobility is improved further.
Accompanying surface modifier can be one or two or more kinds (containing two kinds) mixture in organic system or inorganic system modifying agent,
Described organic system modifying agent, such as (but not limited to): metal soaps such as magnesium stearate, calcium stearate, zinc stearate, barium stearate, lithium stearates; Tissuemat E, lauric acid acid amide, nutmeg acid amide, palm fibre put the synthetic wax classes such as acid amide, stearmide, hardened castor oil; Polyacrylamide, polyimides, nylon, poly-methyl methacrylate vinegar, polyethylene or politef etc.
Described inorganic system modifying agent, such as (but not limited to): Talcum, Muscovitum, bentonite, sericite, white carbon black, curing aluminum, tungsten disulfide, fluorographite, calcium fluoride, boron nitride, silicon dioxide, aluminium oxide, Muscovitum, calcium carbonate, calcium hydroxide, calcium phosphate, magnesium hydroxide, magnesium phosphate, barium sulfate, titanium dioxide are admired, zinc oxide, ceramic bead, bead or crystal pearl etc.
The adhesion amount (being attached to heat-swellable microsphere surface) of described surface modifier is not particularly limited. But if it is considered that the function etc. of surface modifier can be played fully, count with unattached heat-swellable microsphere gross weight for 100 parts by weight, the adhesion amount of described surface modifier is 0.1-95 parts by weight, it is preferably 0.5-60 parts by weight, more preferably 5-50 parts by weight, it is most preferred that for 8-30 parts by weight.
The attachment of surface modifier can be undertaken by the unattached heat-swellable microsphere of mixing and surface modifier. For mixing, it does not have be particularly limited to, can carry out in the container have agitating device. Alternatively, it is also possible to use the powder mixer that can carry out common shake or stirring. As powder mixer, for instance zonate frond type mixer, vertical spin type mixer etc. can be enumerated and can carry out the powder mixer of shake stirring or stirring. Alternatively, it is also possible to use in recent years by the multi-functional powder mixer in hgher efficiency of combination agitating device and super mixer and high-speed mixer, SV mixer etc.
Thermo-expandable microspheres provided by the present invention can be used for papermaking, printing-ink (such as water-based inks, solvent-based ink, plastisol, uv curing ink etc.), putty, sealant, ultralight clay, base coat, binding agent, the degumming of binding agent, artificial leather, corium, paint, nonwoven fabric material, paper and plate, for various materials such as paper, plate, plastics, the coating (such as nonskid coating etc.) of metal and fabric, explosive, cable insulation, thermoplastic (such as polyethylene, polrvinyl chloride and ethane-acetic acid ethyenyl ester) or thermoplastic elastomer (TPE) (such as styrene-ethylene-butylene-styrene copolymer, styrene-butadiene-styrene, thermoplastic polyurethane and TPO), butadiene-styrene rubber, natural rubber, vulcanite, silicone rubber, thermosetting polymer (such as epoxy resin, polyurethane and polyester) etc. field.
The present invention is further elaborated by the examples below. In listed embodiment, except as otherwise noted, in embodiment, all numbers and percentage rate refer to number by weight and percentage rate, and the analysis of heat-swellable microsphere adopts following method and instrument:
(1) particle size distribution profiles analysis:
The particle size distribution of microsphere is that the particle size distribution sub laser diffraction analyzer LS13320 produced by Bekmancoulter company is measured. Average diameter is measured as volume average particle size, and particle size distribution is calculated as C.V. value (standard deviation/average diameter) X100.
(2) foam characteristics analysis:
The thermomechanical analyzer TMAQ-400 that the characteristic of heat-expandable microsphere is produced by TAInstrument company measures.
Sample is prepared by the 1.0mg heat-expandable microsphere held in the aluminum dish of diameter 6.7mm and degree of depth 4.5mm. Then, the aluminum dish of described aluminum dish diameter 6.5mm and degree of depth 4.0mm seals. According to TMA expanding probe type, sample temperature is increased to 230 DEG C with the programming rate of 50 DEG C/min from ambient temperature, and is applied the power of 0.5N by probe. Analyze and undertaken by measuring probe vertical displacement.
-expanding initial temperature (Tstart): probe displacement starts the temperature (DEG C) when increasing.
-foaming maximum temperature (Tmax): the temperature (DEG C) when probe displacement reaches maximum.
-maximum foaming displacement ((Dmax): the displacement (��m) when probe displacement reaches maximum.
Embodiment 1
By mixing 140 grams of acrylonitrile, 20 grams of N, N-DMAA, 40 grams of methyl methacrylates, 0.1 gram of methacrylic acid-2,2,2-trifluoro ethyl esters, 0.4 gram of trimethylol-propane trimethacrylate, 4 grams of benzoyl peroxides and 50 grams of isobutyltrimethylmethane .s obtain the oil phase of suspension polymerisation.
Adding 280 grams of deionized waters, 30 grams of sodium hydroxide in No. 1 beaker, 40 grams of sodium chloride and 0.2 gram of sodium lauryl sulphate fully dissolve; Adding 280 grams of deionized waters, 85 grams of Magnesium dichloride hexahydrates, 30 grams of sodium chloride in No. 2 beakers, the sodium nitrite of 0.01 gram is fully dissolved; First the solution in No. 1 beaker is poured in 2.5 liters of there-necked flasks with stirring paddle, then under 1200rpm rotating speed stirs, then be slowly added to the solution in No. 2 beakers in this there-necked flask. It is sufficiently stirred for again after adding 15 minutes, obtains the aqueous phase of suspension polymerisation.
Oil phase and aqueous phase is disperseed, thus preparing aaerosol solution by stirring 2 minutes under 7000rpm with homogeneous mixer. Injecting in 1 liter of autoclave by aaerosol solution at once, logical nitrogen replaces air, and to reactor supercharging to reach the initial pressure of 0.3MPa. Then, at 69-71 DEG C, polyreaction is carried out 20 hours. After being polymerized, obtain object (heat-swellable microsphere of the present invention) by filtering, wash, drying. The performance of object is in Table 2.
Embodiment 2
By mixing 40 grams of acrylonitrile, 2 grams of N, N-DMAA, 3 grams of methyl methacrylates, 4 grams of acrylic acid methyl ester .s, 0.1 gram of methacrylic acid-2,2,2-trifluoro ethyl esters, 0.5 gram of methacrylic acid, 0.1 gram of acrylic acid, 0.4 gram of trimethylol-propane trimethacrylate, 1 gram of azodiisobutyronitrile, 12 grams of isobutyltrimethylmethane .s and 3 grams of isopentane obtain the oil phase of suspension polymerisation.
In 200 weight portion ion exchange waters, add 23 parts by wt NaCl, 10 weight portions (effective ingredient amount: 20 weight %) silica sol, 0.1 weight account polyethylene ketopyrrolidine and 0.01 weight portion sodium nitrite, then by pH regulator to 2.4, mix equably, it can be used as aqueous dispersion medium.
Oil phase and aqueous phase is disperseed, thus preparing aaerosol solution by stirring 3 minutes under 6000rpm with homogeneous mixer. Injecting in 1 liter of autoclave by aaerosol solution at once, logical nitrogen replaces air, and to reactor supercharging to reach the initial pressure of 0.3MPa. Then, at 60-61 DEG C, polyreaction is carried out 20 hours. After being polymerized, obtain object (heat-swellable microsphere of the present invention) by filtering, wash, drying. The performance of object is in Table 2.
Embodiment 3-6
Except the kind changing monomer used, cross-linking agent, initiator and expandable substance and consumption and polymer temperature (referring specifically to table 1), other condition is identical with embodiment 1, prepares different heat-swellable microspheres, and its performance is in Table 2.
Table 1
In table 1, AN: acrylonitrile, MMA: methyl methacrylate, DMAA:N, N-DMAA, AM: acrylamide, HMAA:N-n-methylolacrylamide, TFEMA: trifluoroethyl methacrylate, HFBA: hexafluorobutyl acrylate, TMPDMA: trimethylol-propane trimethacrylate, EGDMA: Ethylene glycol dimethacrylate, DEGDE: diethylene glycol divinyl ether, BPO: benzoyl peroxide, AIBN: azodiisobutyronitrile, LPO: lauroyl peroxide, DCPD: peroxidating dicyclohexyl carbonate, IO: isobutyltrimethylmethane., NH: normal hexane, IP: isopentane.
Table 2
Comparative example 1��3
Except the kind changing monomer used, cross-linking agent, initiator and expandable substance and consumption and polymer temperature (referring specifically to table 1), other condition is identical with embodiment 1, prepares different heat-swellable microspheres, and its performance is in Table 2.
By table 1 with table 2 it can be seen that compare with comparative example 1-3, the embodiment 1-6 including N,N-DMAA (DMAA) and the monomer mixture of trifluoroethyl methacrylate shows the foam characteristics significantly improved, and has narrow particle size distribution.
Comparative examples 1 and 2, when replacing part AN as monomer with DMAA, and when being not added with trifluoroethyl methacrylate, TStartAnd TMaximumSignificantly improve, but particle size distribution is substantially wider.
Additionally, for only using trifluoroethyl methacrylate to be not added with the comparative example 3 of DMAA, although narrow particle size distribution, but TStartAnd TMaximumDo not significantly improve.
Method given according to the above description, those skilled in the art are it is conceivable that the multiple amendment of the present invention and other embodiments. It will thus be appreciated that protection scope of the present invention is not limited to the embodiment disclosed, protection scope of the present invention is set forth in the claims.

Claims (15)

1. a heat-swellable thermoplastic microspheres, it mainly can be gathered monomer by olefinic and expandable substance obtains through suspension polymerisation, obtained heat-swellable thermoplastic microspheres be with thermoplastic polymer for shell and be core with expandable substance the microsphere with nucleocapsid structure, it is characterized in that, wherein said olefinic can gather monomer by acrylonitrile, acrylic ester monomer, acrylamide monomers, acrylate containing fluorine monomer and acrylic monomer composition, the gross weight of monomer can be gathered for 100wt% for calculating benchmark with described olefinic, can gather in monomer at described olefinic, acrylonitrile accounts for 30wt%��90wt%, methacrylate-based monomer accounts for 5wt%��50wt%, acrylamide monomers accounts for 1wt%��20wt%, acrylate containing fluorine monomer accounts for 0.01wt%��1.0wt%, acrylic monomer accounts for 0wt%��40wt%,
Wherein, described methacrylate-based monomer is selected from: the mixture of one or two or more kinds in compound race described in Formulas I, described acrylamide monomers is selected from: the mixture of one or two or more kinds in compound race described in Formula II, described acrylate containing fluorine monomer is selected from: the mixture of one or two or more kinds in compound race described in formula III, described acrylic monomer is acrylic acid or/and methacrylic acid
The boiling point of described expandable substance not higher than the softening temperature of prepared thermoplastic polymer,
The polymerization temperature of described suspension polymerisation is 40 DEG C��100 DEG C, and the polymerization gauge pressure of described suspension polymerisation is 0.1MPa��3.0MPa,
In formula, R1For C1��C10Straight chain, side chain or cyclic alkyl, R2And R3It is respectively and independently selected from: H, C1��C6The C that straight or branched alkyl or hydroxyl replace1��C6One, R in straight or branched alkyl4For C1��C6Straight or branched containing fluoroalkyl, R5For H or methyl.
2. heat-swellable thermoplastic microspheres as claimed in claim 1, it is characterised in that wherein said acrylic monomer accounts for 1wt%��30wt%.
3. heat-swellable thermoplastic microspheres as claimed in claim 1 or 2, it is characterised in that with described thermo-expandable microspheres gross weight for 100wt% for calculating benchmark, expandable substance accounts for 5wt%��50wt%.
4. heat-swellable thermoplastic microspheres as claimed in claim 3, it is characterised in that wherein expandable substance accounts for 10wt%��35wt%.
5. heat-swellable thermoplastic microspheres as claimed in claim 4, it is characterised in that wherein said expandable substance C5��C12Aliphatic hydrocarbon compounds.
6. heat-swellable thermoplastic microspheres as claimed in claim 5, it is characterised in that wherein said expandable substance is C5��C8Straight or branched saturated hydrocarbons compound.
7. the heat-swellable thermoplastic microspheres as described in claim 1,2 or 6, it is characterised in that wherein R1For C1��C6Straight or branched alkyl.
8. heat-swellable thermoplastic microspheres as claimed in claim 7, it is characterised in that wherein R1For C1��C3Straight or branched alkyl.
9. heat-swellable thermoplastic microspheres as claimed in claim 8, it is characterised in that wherein R1For methyl.
10. the heat-swellable thermoplastic microspheres as described in claim 1,2 or 6, it is characterised in that wherein R2And R3It is respectively and independently selected from: H, C1��C3The C that straight or branched alkyl or hydroxyl replace1��C3One in straight or branched alkyl.
11. heat-swellable thermoplastic microspheres as claimed in claim 10, it is characterised in that wherein R2And R3It is respectively and independently selected from: a kind of in H, methyl or methylol.
12. heat-swellable thermoplastic microspheres as claimed in claim 11, it is characterised in that acrylamide monomers wherein used is that acrylamide, N hydroxymethyl acrylamide are or/and N,N-DMAA.
13. the heat-swellable thermoplastic microspheres as described in claim 1,2 or 6, it is characterised in that wherein R4For C2��C4Straight or branched containing fluoroalkyl.
14. heat-swellable thermoplastic microspheres as claimed in claim 13, it is characterised in that wherein R4For trifluoroethyl or hexafluoro butyl.
15. heat-swellable thermoplastic microspheres as claimed in claim 1, it is characterised in that wherein the polymerization temperature of suspension polymerisation is 50 DEG C��85 DEG C, and the polymerization gauge pressure of suspension polymerisation is 0.2MPa��2.0MPa.
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