CN102633936A - Thermoexpandable thermoplastic microspheres - Google Patents

Thermoexpandable thermoplastic microspheres Download PDF

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CN102633936A
CN102633936A CN2012101093023A CN201210109302A CN102633936A CN 102633936 A CN102633936 A CN 102633936A CN 2012101093023 A CN2012101093023 A CN 2012101093023A CN 201210109302 A CN201210109302 A CN 201210109302A CN 102633936 A CN102633936 A CN 102633936A
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thermoplastic microspheres
monomer
straight
swellable
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CN102633936B (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 invention relates to thermoexpandable thermoplastic microspheres which are mainly prepared by carrying out suspension polymerization on olefine polymerizable monomers and expandable substances. The thermoexpandable thermoplastic microspheres have a core-shell structure which uses the thermoplastic polymers as the shell and the expandable substances as the cure. The invention is characterized in that on the basis of 100 wt% as the total weight of the olefine polymerizable monomers, the olefine polymerizable monomers are composed of 30-90 wt% of acrylonitrile, 5-50 wt% of methacrylate monomers, 1-20 wt% of acrylamide monomers, 0.01-1.0 wt% of fluorine-containing acrylate monomers and 0-40 wt% of acrylic monomers. The start T of the thermoexpandable thermoplastic microspheres is 160-200 DEG C.

Description

The heat-swellable thermoplastic microspheres
Technical field
The present invention relates to a kind of thermoplastic microspheres of heat-swellable.
Background technology
The thermoplastic microspheres of heat-swellable is a kind of mainly by being shell with the thermoplastic polymer and being the microsphere with nucleocapsid structure that nuclear constituted with the expandable substance.In this type of microsphere, expandable substance normally boiling point is not higher than the liquid of the softening temperature of thermoplastic polymer (shell).Meet heat, said liquid evaporation and increase interior pressure, meanwhile, said thermoplastic polymer (shell) is softening, (the temperature brief note when microballoon begins to expand is T thereby cause said microballoon to expand Beginning, and the temperature brief note when realizing maximum swelling is T Maximum).
In some Application Areass, the user hopes that the thermoplastic microspheres of the heat-swellable that supplier provides has higher T Beginning(generally at 160 ℃-200 ℃).Yet, have a higher T existing BeginningThe thermoplastic microspheres of heat-swellable in; Methacrylonitrile becomes the necessary component that constitutes thermoplastic polymer (shell) (methacrylonitrile complex manufacturing and cost an arm and a leg); Do not having under the condition of methacrylonitrile, the performance of the thermoplastic microspheres of the heat-swellable that makes (mainly is T BeginningAnd swelling capacity) still can not make the user satisfied.
Therefore, provide a kind of that do not contain methacrylonitrile and have a higher T Beginning(generally at 160 ℃-200 ℃) and the heat-swellable thermoplastic microspheres of higher swelling capacity become the technical issues that need to address of the present invention.
Summary of the invention
The objective of the invention is to, provide a kind of that do not contain methacrylonitrile and have a higher T BeginningThe heat-swellable thermoplastic microspheres of (generally at 160 ℃-200 ℃) and higher swelling capacity.
Heat-swellable thermoplastic microspheres provided by the present invention; It mainly can gather monomer by olefinic and expandable substance obtains through suspension polymerization; Resulting heat-swellable thermoplastic microspheres is to be shell with the thermoplastic polymer and to be the microballoon with nucleocapsid structure of nuclear with the expandable substance; It is characterized in that wherein said olefinic can gather monomer and be made up of vinyl cyanide, acrylic ester monomer, acrylamide monomers, acrylate containing fluorine monomer and acrylic monomer, can gather monomeric gross weight with said olefinic is that 100wt% calculates benchmark; Can gather in the monomer at described olefinic; Vinyl cyanide accounts for 30wt%~90wt%, and the methyl acrylic ester monomer accounts for 5wt%~50wt%, and acrylamide monomers accounts for 1wt%~20wt%; The acrylate containing fluorine monomer accounts for 0.01wt%~1.0wt%, and acrylic monomer accounts for 0wt%~40wt% (preferred 1wt%~30wt%);
Wherein, Said acrylic ester monomer is selected from: mixture a kind of or that (contain two kinds) more than two kinds in the said compound of the formula I family; Said acrylamide monomers is selected from: mixture a kind of or that (contain two kinds) more than two kinds in the said compound of the formula II family; Said acrylate containing fluorine monomer is selected from: mixture a kind of or that (contain two kinds) more than two kinds in the said compound of the formula III family, and said acrylic monomer is that vinylformic acid is or/and methylacrylic acid;
Figure BSA00000701213400021
In the formula, R 1Be C 1~C 10Straight chain, side chain or cyclic alkyl, R 2And R 3Independently be selected from respectively: H, C 1~C 6The substituted C of straight or branched alkyl or hydroxyl 1~C 6A kind of in the straight or branched alkyl, R 4Be C 1~C 6Straight or branched contain fluoroalkyl, R 5Be H or methyl.
The present invention mainly substitutes methacrylonitrile (monomer) in the prior art with acrylamide monomers and acrylate containing fluorine monomer, has obtained to have higher T BeginningThe heat-swellable thermoplastic microspheres of (generally at 160 ℃-200 ℃) and higher swelling capacity reaches intended purposes of the present invention.
Embodiment
The thermoplastic microspheres for preparing heat-swellable according to the invention can adopt existing suspension polymerization.In described suspension polymerization, expandable substance keeps suspended state with the polymerizable compound that comprises polymerisable monomer through continuously stirring or interpolation dispersion stabilizer (like Marinco H or colloid silica etc.).Through suspension polymerization, polymkeric substance can form sphere.
In the present invention, to initiator used in used expandable substance and the suspension polymerization and linking agent and have no special requirements.
For the selection of expandable substance, as long as satisfy the softening temperature that the boiling point of selecteed expandable substance is not higher than the prepared thermoplastic polymer of the present invention (shell).The present invention recommends to use C 5~C 12The aliphatic hydrocarbon compounds, preferred expandable substance is C 5~C 12The straight or branched saturated hydrocarbons compound, further preferred expandable substance is C 5~C 8The straight or branched saturated hydrocarbons compound.
For the selection of linking agent, be fit to linking agent of the present invention and be to contain a kind of compound of or the bridging property official group that (contains two kinds) more than two kinds, concrete linking agent is selected from a kind of or mixture that (contains two kinds) more than two kinds in the following compounds:
Vinylstyrene, ethylene glycol bisthioglycolate (methyl) propenoate, two (terepthaloyl moietie) two (methyl) propenoate, triethylene glycol two (methyl) propenoate, Ucar 35 two (methyl) propenoate, 1; 4-butyleneglycol two (methyl) propenoate, 1; 6-pinakon two (methyl) propenoate, glycerine two (methyl) propenoate, 1; 3-butyleneglycol two (methyl) propenoate, NSC 6366 two (methyl) propenoate, decamethylene-glycol two (methyl) propenoate, tetramethylolmethane three (methyl) propenoate, tetramethylolmethane four (methyl) propenoate, Dipentaerythritol six (methyl) propenoate, triallyl formal three (methyl) propenoate, allyl methacrylate(AMA), trimethylolpropane tris (methyl) propenoate, three butyleneglycol two (methyl) propenoate, PEG#200 two (methyl) propenoate, PEG#400 two (methyl) propenoate, PEG#600 two (methyl) propenoate, 3 acrylic acid oxygen base glycol mono acrylic ester, three acyl group formals, triallyl isocyanate, cyanacrylate, divinyl ether, ethylene glycol bisthioglycolate vinyl ether, Diethylene Glycol divinyl ether, triethylene glycol divinyl ether or TEG divinyl ether etc.
The consumption of linking agent is the 0.1wt%~10wt% of the total monomer weight that is used to prepare thermoplastic polymer (shell), and its preferred consumption is the 0.1wt%~3wt% of the total monomer weight that is used to prepare thermoplastic polymer (shell).
For the selection of initiator, the existing initiator (like organic superoxide or azo compound etc.) that is used for radical polymerization all is fit to the present invention, and concrete initiator is selected from a kind of or mixture that (contains two kinds) more than two kinds in the following compounds:
Two (hexadecyl) peroxy dicarbonate, two (4-tert-butylcyclohexyl) peroxy dicarbonate, peroxo-are two sad, diphenyl peroxide formic acid, peroxo-two LAURIC ACID 99 MIN, peroxo-two capric acid, tertiary butyl peroxy acetic acid ester, the tertiary butyl are crossed laurate, tert butyl peroxy benzoate, t-butyl hydroperoxide, cumene hydroperoxide, ethyl cumene peroxide, di-isopropyl hydroxydicarboxylic acid ester, 2; 2 '-azo two ((2; The 4-methyl pentane nitrile), 2; 2 '-azo two (isopropyl cyanide), 1; 1 '-azo two (hexanaphthene-1-nitrile), dimethyl-2; 2 ,-azo two (2 Methylpropionic acid ester) or 2,2 '-azo two [2-methyl-N-(2-hydroxyethyl)-propionic acid amide] etc.
Can decide according to the kind of used initiator as for described suspension polymerization temperatures, the suspension polymerization temperatures that the present invention recommends is 40 ℃~100 ℃, and preferred suspension polymerization temperatures is 45 ℃~90 ℃, and preferred suspension polymerization temperatures is 50 ℃~85 ℃.
For polymerization initial stage pressure, preferred gauge pressure is 0-5.0MPa, and then preferred 0.1-3.0MPa, preferred especially 0.2-2.0MPa.
In addition, preferably make in its aqueous dispersion medium that is containing dispersion stabilizer and/or stably dispersing auxiliary agent in the present invention and carry out suspension polymerization.Usage quantity for described aqueous dispersion medium does not have special qualification, with respect to the polymerizable components (can gather the monomer total amount) of 100 weight parts, preferably uses the aqueous dispersion medium of 100 weight part to 1000 weight parts.
Wherein said dispersion stabilizer can be that colloid silica, colloid lime carbonate, Marinco H, calcium phosphate, white lake, ironic hydroxide, calcium sulfate, sodium sulfate, caoxalate, lime carbonate, barium carbonate, magnesiumcarbonate are or/and alumina sol etc.The consumption of dispersion stabilizer is preferably the 0.1wt%~20wt% of polymerizable components (can gather the monomer total amount) gross weight.
Further; Above-mentioned stably dispersing auxiliary agent can be selected from: the stably dispersing auxiliary agent of polymers such as the condensation resultant of diethylolamine and aliphatic dicarboxylic acid, gelatin, Vinylpyrrolidone polymer, methylcellulose gum, polyethylene oxide, Z 150PH; Cats products such as alkyltrimethylammonium chloride or chlorination dialkyl dimethyl ammonium; ASs such as sodium alkyl sulfate, various emulsifying agents such as zwitterionics such as alkyl dimethyl aminoacetic acid trimethyl-glycine, alkyl dihydroxy ethyl aminoacetic acid trimethyl-glycine.The consumption of stably dispersing auxiliary agent is preferably the 0.001wt%~2.0wt% of polymerizable components (can gather the monomer total amount) gross weight.
The pH of the aqueous dispersion medium during polymerization suitably determines according to the kind of the dispersion stabilizer that uses.For example; If dispersion stabilizer is selected from: the salt of metal Ca, Mg, Ba, Zn, Ni and Mn, oxide compound or oxyhydroxide are (concrete like calcium phosphate, lime carbonate, Marinco H, Natural manganese dioxide, permanent white, caoxalate; With a kind of in the oxyhydroxide of zinc, nickel or manganese or the mixture that (contains two kinds) more than two kinds); The then preferred 5-12 of pH value, more preferably 6-10; If dispersion stabilizer is selected from: the oxide compound or the oxyhydroxide of starch, methylcellulose gum, Vltra tears, carboxyl methylcellulose, glue agar, colloid silica, colloidal clays or aluminium or iron, the then preferred 1-6 of pH value, more preferably 3-5.
In addition, in aqueous dispersion medium, also can contain water-soluble radical suppressor factor, to suppress the generation of the cohesion microballoon in the polymerization.As water-soluble radical suppressor factor, can be nitrite alkali metal-salt (Sodium Nitrite and/or potassium nitrite etc.), dichromate (ammonium dichromate (two ammonium chromates), sodium dichromate 99 (two Sodium chromate-51Crs) and/or SRM 935a (two potassiumchromates) etc.); Tin protochloride; Tin chloride, iron protochloride, iron(ic)chloride; Ferrous sulfate, radical suppressor factor such as water-soluble xitix class and verivate thereof.Aspect the stability water, preferred nitrite alkali metal-salt.Per 100 parts by weight polymerizable components (can gather the monomer total amount), the consumption of water-soluble radical suppressor factor is the 0.0001-1 parts by weight, preferred 0.0003-0.1 parts by weight.
In the used aqueous dispersion medium of the present invention, also can contain ionogen.Do not have special qualification for ionogen, as being selected from: lithium chloride, sodium-chlor, Repone K, magnesium chloride, calcium chloride, sodium hydrogencarbonate, Lithium Sulphate, sodium sulfate, vitriolate of tartar, sal epsom, sulfuric acid are a kind of or (contain two kinds) more than two kinds by, yellow soda ash or TRIMETHOXY BENZOIC ACID (FOR MANUFACTURING OF T.M. etc.With respect to the aqueous dispersion medium of 100 parts by weight, electrolytical consumption is advisable with the 0.1-50 parts by weight.
The mean diameter of heat-swellable microballoon provided by the present invention is 5 μ m~100 μ m, and preferred mean diameter is 10 μ m~100 μ m, further preferred mean diameter 10 μ m~60 μ m.
In addition; With the heat-swellable microballoon gross weight that is provided is that 100wt% calculates benchmark, and expandable substance accounts for 5wt%~50wt%, and preferred content is 10wt%~50wt%; Further preferred content is 10wt%~40wt%, and the optimum content of expandable substance is 10wt%~35wt%.
In another optimized technical scheme of the present invention, R 1Be C 1~C 6The straight or branched alkyl, preferred R 1Be C 1~C 3The straight or branched alkyl, best R 1Be methyl.
In another optimized technical scheme of the present invention, R 2And R 3Independently be selected from respectively: H, C 1~C 3The substituted C of straight or branched alkyl or hydroxyl 1~C 3A kind of in the straight or branched alkyl, preferred R 2And R 3Independently be selected from respectively: a kind of in H, methyl or the methylol, compound is acrylic amide, N hydroxymethyl acrylamide or N shown in the best formula II, the N-DMAA.
In another optimized technical scheme of the present invention, R 4Be C 2~C 4Straight or branched contain fluoroalkyl, best R 4Be trifluoroethyl or hexafluoro butyl.
When polymerization is accomplished basically, can obtain the microballoon of water paste or dispersion-s, they can in statu quo use or obtain so-called wet cake through any ordinary method (for example bed filter, press filtration, leaf filter, commentaries on classics filter, band filter or centrifugal the dehydration).Yet, also can be through any ordinary method (for example spraying drying, support drying, tunnel drying, Rotary drying, drum dried, air seasoning, turbine support are dry, disk is dry or fluidised bed drying etc.), with this microspheres drying.
But also attaching surface properties-correcting agent, the further raising that realization is dispersed or mobile further improvement of outside surface at heat-swellable property microballoon provided by the present invention.
The surface-modifying agent that is adhered to can for organic system or inorganic be a kind of or mixture that (contains two kinds) more than two kinds in the properties-correcting agent,
Said organic system properties-correcting agent is like (but being not limited to): metallic soap classes such as Magnesium Stearate, calcium stearate, Zinic stearas, barium stearate, lithium stearates; Polyethylene wax, LAURIC ACID 99 MIN acid amide, nutmeg acid acid amides, palm fibre are put synthetic wax classes such as sour acid amides, stearylamide, hardened castor oil; SEPIGEL 305, polyimide, nylon, poly-methyl methacrylate vinegar, Vilaterm or tetrafluoroethylene etc.
Said inorganic be properties-correcting agent, like (but being not limited to): talcum, mica, wilkinite, sericite, carbon black, curing aluminium, tungsten disulfide, fluorographite, Calcium Fluoride (Fluorspan), SP 1, silicon-dioxide, aluminum oxide, mica, lime carbonate, calcium hydroxide, calcium phosphate, Marinco H, trimagnesium phosphate, permanent white, titanium dioxide are admired, zinc oxide, ceramic bead, granulated glass sphere or crystal pearl etc.
Do not limit the adhesion amount (attached to heat-swellable property microsphere surface) of said surface-modifying agent is special.If but consider the function that to bring into play surface-modifying agent fully etc.; Heat-swellable property microballoon gross weight not adhere to is 100 parts by weight; The adhesion amount of said surface-modifying agent is the 0.1-95 parts by weight; Be preferably the 0.5-60 parts by weight, further be preferably the 5-50 parts by weight, most preferably be the 8-30 parts by weight.
Adhering to of surface-modifying agent can be carried out through mixing the heat-swellable property microballoon and the surface-modifying agent that do not adhere to.For mixing, not special the qualification can be carried out in having the container of whipping appts.In addition, also can use and to carry out the common powder mixing machine that shakes or stir.As the powder mixing machine, for example can enumerate zonate frond type mixing machine, vertical spin type mixing machine etc. and can shake the powder mixing machine that stirs or stir.In addition, also can use is super mixing machine and high-speed mixer, SV mixing machine etc. through the higher multi-functional powder mixing machine of efficient that makes up whipping appts in recent years.
Heat-swellable microballoon provided by the present invention can be used for papermaking, printing-ink (for example water-based inks, solvent-based ink, plastisol, uv curing ink etc.), putty, sealing agent; The ultralight clay, base coat, tackiness agent; Coming unstuck of tackiness agent, leatheroid, corium; Paint, nonwoven fabric material, paper and plate; The coating (like nonskidcoating etc.) that is used for various materials such as paper, plate, plastics, metal and fabric, explosive substance, cable insulation; Thermoplastics (for example Vilaterm, SE and ethane-acetic acid ethyenyl ester) or thermoplastic elastomer (for example styrene-ethylene-butylene-styrene multipolymer, styrene-butadiene-styrene multipolymer, thermoplastic polyurethane and TPO), styrene-butadiene rubber(SBR), tree elastomer; Vulcanized rubber, silicone rubber, thermosetting polymer fields such as (for example epoxy resin, urethane and polyester).
Through embodiment the present invention is done further elaboration below.In listed embodiment, except as otherwise noted, all umbers and percentage are meant by weight umber and percentage among the embodiment, and following method and instrument are adopted in the analysis of heat-swellable property microballoon:
(1) size distribution specificity analysis:
The size distribution of microballoon is to measure through the size distribution laser diffraction analysis appearance LS13320 that Bekman coulter company produces.Mean diameter is measured as volume average particle size, and size distribution is calculated as C.V. value (standard deviation/mean diameter) X100.
(2) foaming character analysis:
The characteristic of heat-expandable microsphere is measured through the thermomechanical analyzer TMA Q-400 that TA Instrument company produces.
The 1.0mg heat-expandable microsphere that holds in the aluminium dish by diameter 6.7mm and degree of depth 4.5mm prepares sample.Then, said aluminium dish is with the aluminium dish sealing of diameter 6.5mm and degree of depth 4.0mm.According to TMA expanding probe type, sample temperature is increased to 230 ℃ with the heat-up rate of 50 ℃/min from envrionment temperature, and applies the power of 0.5N by probe.Analysis is carried out through the measuring sonde vertical translation.
-expansion initial temperature (Tstart): the temperature when the probe displacement begins to increase (℃).
-foaming top temperature (Tmax): the temperature when the probe displacement reaches maximum (℃).
-maximum foaming displacement ((Dmax): the displacement (μ m) when the probe displacement reaches maximum.
Embodiment 1
Through mixing 140 gram vinyl cyanide, 20 gram N; N-DMAA, 40 gram TEB 3Ks, 0.1 gram methylacrylic acid-2; 2,2-trifluoro ethyl ester, 0.4 gram trimethylolpropane trimethacrylate, 4 gram Lucidols and 50 gram octane-iso obtain the oil phase of suspension polymerization.
In No. 1 beaker, add 280 gram deionized waters, 30 gram sodium hydroxide, 40 gram sodium-chlor and 0.2 gram sodium lauryl sulphate are fully dissolved; In No. 2 beakers, add 280 gram deionized waters, 85 gram Magnesium dichloride hexahydrates, 30 gram sodium-chlor, the Sodium Nitrite of 0.01 gram fully dissolves; Earlier the solution in No. 1 beaker is poured in 2.5 liters of there-necked flasks that have stirring rake, stirred down at the 1200rpm rotating speed then, the more slow solution in No. 2 beakers of adding in this there-necked flask.Fully stirred again 15 minutes after adding, obtain the water of suspension polymerization.
Disperseed oil phase and water in 2 minutes through under 7000rpm, stirring with the intimate mixing machine, thus the preparation aaerosol solution.At once aaerosol solution is injected 1 and raises and press reaction kettle, logical nitrogen replacement air, and to the reaction kettle supercharging to reach the original pressure of 0.3MPa.Then, under 69-71 ℃, carried out polyreaction 20 hours.Polymerization obtains target compound (heat-swellable property microballoon of the present invention) through filtration, washing, drying after accomplishing.The performance of target compound is seen table 2.
Embodiment 2
Through mixing 40 gram vinyl cyanide, 2 gram N; N-DMAA, 3 gram TEB 3Ks, 4 gram methyl acrylates; 0.1 gram methylacrylic acid-2; 2,2-trifluoro ethyl ester, 0.5 gram methylacrylic acid, 0.1 gram vinylformic acid, 0.4 gram trimethylolpropane trimethacrylate, 1 gram Diisopropyl azodicarboxylate, 12 gram octane-iso and 3 gram iso-pentane obtain the oil phase of suspension polymerization.
In 200 weight part ion exchanged waters; Add 23 weight part sodium-chlor, 10 weight parts (effective constituent amount: 20 weight %) colloid silica, 0.1 weight account polyethylene pyrrolidone and 0.01 weight part Sodium Nitrite; Then with pH regulator to 2.4; Mix equably, with it as aqueous dispersion medium.
Disperseed oil phase and water in 3 minutes through under 6000rpm, stirring with the intimate mixing machine, thus the preparation aaerosol solution.At once aaerosol solution is injected 1 and raises and press reaction kettle, logical nitrogen replacement air, and to the reaction kettle supercharging to reach the original pressure of 0.3MPa.Then, under 60-61 ℃, carried out polyreaction 20 hours.Polymerization obtains target compound (heat-swellable property microballoon of the present invention) through filtration, washing, drying after accomplishing.The performance of target compound is seen table 2.
Embodiment 3-6
Except that the kind and consumption and polymer temperature that change used monomer, linking agent, initiator and expandable substance (specifically referring to table 1), other condition is identical with embodiment 1, makes different heat-swellable property microballoons, and its performance is seen table 2.
Table 1
Figure BSA00000701213400071
In the table 1, AN: vinyl cyanide, MMA: TEB 3K, DMAA:N; The N-DMAA, AM: acrylic amide, HMAA:N-NMA, TFEMA: trifluoroethyl methacrylate; HFBA: vinylformic acid hexafluoro butyl ester, TMPDMA: trimethylolpropane trimethacrylate, EGDMA: TGM 1, DEGDE: Diethylene Glycol divinyl ether; BPO: Lucidol, AIBN: Diisopropyl azodicarboxylate, LPO: lauroyl peroxide, DCPD: peroxo-carbonic acid two cyclohexyls; IO: octane-iso, NH: normal hexane, IP: iso-pentane.
Table 2
Figure BSA00000701213400081
Comparative example 1~3
Except that the kind and consumption and polymer temperature that change used monomer, linking agent, initiator and expandable substance (specifically referring to table 1), other condition is identical with embodiment 1, makes different heat-swellable property microballoons, and its performance is seen table 2.
Can know that by table 1 and table 2 1-3 compares with comparative example, comprise N, the foaming character that the embodiment 1-6 performance of the monomer mixture of N-DMAA (DMAA) and trifluoroethyl methacrylate significantly improves, and have narrow size distribution.
Comparative examples 1 and 2, when with DMAA instead of part AN as monomer, and not during methylate vinylformic acid trifluoro ethyl ester, T Open BeginningAnd T MaximumObviously improve, but the obvious broad of size distribution.
In addition, do not add the comparative example 3 of DMAA for only using trifluoroethyl methacrylate, though size distribution narrows down T BeginningAnd T MaximumObviously do not improve.
The method given according to above-mentioned explanation, those skilled in the art can expect multiple modification of the present invention and other embodiments.Therefore, should be appreciated that the embodiment that protection scope of the present invention is not limited to disclose, protection scope of the present invention is set forth in claim.

Claims (15)

1. heat-swellable thermoplastic microspheres; It mainly can gather monomer by olefinic and expandable substance obtains through suspension polymerization, and resulting heat-swellable thermoplastic microspheres is to be shell with the thermoplastic polymer and to be the microballoon with nucleocapsid structure of nuclear with the expandable substance, it is characterized in that; Wherein said olefinic can gather monomer and be made up of vinyl cyanide, acrylic ester monomer, acrylamide monomers, acrylate containing fluorine monomer and acrylic monomer; Can gather monomeric gross weight with said olefinic is that 100wt% calculates benchmark, can gather in the monomer at described olefinic, and vinyl cyanide accounts for 30wt%~90wt%; The methyl acrylic ester monomer accounts for 5wt%~50wt%; Acrylamide monomers accounts for 1wt%~20wt%, and the acrylate containing fluorine monomer accounts for 0.01wt%~1.0wt%, and acrylic monomer accounts for 0wt%~40wt%;
Wherein, Said methyl acrylic ester monomer is selected from: a kind of or mixture more than two kinds in the said compound of the formula I family; Said acrylamide monomers is selected from: a kind of or mixture more than two kinds in the said compound of the formula II family; Said acrylate containing fluorine monomer is selected from: a kind of or mixture more than two kinds in the said compound of the formula III family, said acrylic monomer are that vinylformic acid is or/and methylacrylic acid
The boiling point of said expandable substance is not higher than the softening temperature of prepared thermoplastic polymer,
The polymerization temperature of said suspension polymerization is 40 ℃~100 ℃, and the polymerization gauge pressure of said suspension polymerization is 0.1MPa~3.0MPa,
Figure FSA00000701213300011
In the formula, R 1Be C 1~C 10Straight chain, side chain or cyclic alkyl, R 2And R 3Independently be selected from respectively: H, C 1~C 6The substituted C of straight or branched alkyl or hydroxyl 1~C 6A kind of in the straight or branched alkyl, R 4Be C 1~C 6Straight or branched contain fluoroalkyl, R 5Be H or methyl.
2. heat-swellable thermoplastic microspheres as claimed in claim 1 is characterized in that wherein said acrylic monomer accounts for 1wt%~30wt%.
3. according to claim 1 or claim 2 heat-swellable thermoplastic microspheres is characterized in that, is that 100wt% calculates benchmark with said heat-swellable microballoon gross weight, and expandable substance accounts for 5wt%~50wt%.
4. heat-swellable thermoplastic microspheres as claimed in claim 3 is characterized in that wherein expandable substance accounts for 10wt%~35wt%.
5. heat-swellable thermoplastic microspheres as claimed in claim 4 is characterized in that, wherein said expandable substance C 5~C 12The aliphatic hydrocarbon compounds.
6. heat-swellable thermoplastic microspheres as claimed in claim 5 is characterized in that wherein said expandable substance is C 5~C 8The straight or branched saturated hydrocarbons compound.
7. like claim 1,2 or 6 described heat-swellable thermoplastic microspheres, it is characterized in that, wherein R 1Be C 1~C 6The straight or branched alkyl.
8. heat-swellable thermoplastic microspheres as claimed in claim 7 is characterized in that, wherein R 1Be C 1~C 3The straight or branched alkyl.
9. heat-swellable thermoplastic microspheres as claimed in claim 8 is characterized in that, wherein R 1Be methyl.
10. like claim 1,2 or 6 described heat-swellable thermoplastic microspheres, it is characterized in that, wherein R 2And R 3Independently be selected from respectively: H, C 1~C 3The substituted C of straight or branched alkyl or hydroxyl 1~C 3A kind of in the straight or branched alkyl.
11. heat-swellable thermoplastic microspheres as claimed in claim 10 is characterized in that, wherein R 2And R 3Independently be selected from respectively: a kind of in H, methyl or the methylol.
12. heat-swellable thermoplastic microspheres as claimed in claim 11 is characterized in that, wherein used acrylamide monomers is acrylic amide, N hydroxymethyl acrylamide or/and N, the N-DMAA.
13., it is characterized in that, wherein R like claim 1,2 or 6 described heat-swellable thermoplastic microspheres 4Be C 2~C 4Straight or branched contain fluoroalkyl.
14. heat-swellable thermoplastic microspheres as claimed in claim 13 is characterized in that, wherein R 4Be trifluoroethyl or hexafluoro butyl.
15. like any described heat-swellable thermoplastic microspheres in the claim 1~14, it is characterized in that wherein the polymerization temperature of suspension polymerization is 50 ℃~85 ℃, the polymerization gauge pressure of suspension polymerization is 0.2MPa~2.0MPa.
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CN105693908A (en) * 2016-02-17 2016-06-22 湖南方锐达科技有限公司 Method for wrapping thermal-expandable microspheres again
CN107459671A (en) * 2017-08-22 2017-12-12 成都新柯力化工科技有限公司 A kind of modified expanded microballoon for polypropylene plastics foaming and preparation method thereof
CN107739492A (en) * 2017-09-26 2018-02-27 西能化工科技(上海)有限公司 Light resilient solid tyre and preparation method thereof
CN107915799A (en) * 2017-10-23 2018-04-17 陈晨特 A kind of new and effective microspheres and preparation method thereof
CN108097182A (en) * 2018-01-05 2018-06-01 三明市锦浪新材料科技有限公司 A kind of ultra-fine environment protection thermal expanding microcapsules and preparation method thereof
CN108218372A (en) * 2017-12-08 2018-06-29 西能化工科技(上海)有限公司 Ultralight energy-storage gypsum plate and preparation method thereof
CN108699422A (en) * 2016-02-19 2018-10-23 松本油脂制药株式会社 Heat-expandable microsphere and application thereof
CN108770358A (en) * 2015-12-31 2018-11-06 聚合物胶粘剂密封胶系统公司 System and method for the flexible sealing agent with density modifier
CN108912384A (en) * 2018-07-20 2018-11-30 西能化工科技(上海)有限公司 Superhigh temperature expandable thermoplastic microspheres and its preparation method and application
CN108912383A (en) * 2018-07-20 2018-11-30 西能化工科技(上海)有限公司 Superhigh temperature expandable thermoplastic microspheres and its application
CN109749534A (en) * 2019-01-10 2019-05-14 西能化工科技(上海)有限公司 Automobile PVC stone-impact-proof paint and preparation method thereof
CN109970466A (en) * 2019-03-29 2019-07-05 东莞市泰赛特汽车用品科技有限公司 A kind of environmental protection brick face antilubricant and preparation method thereof
CN110698721A (en) * 2019-10-15 2020-01-17 江苏科技大学 Polymethacrylimide thermal expansion microsphere and preparation method thereof
CN111116969A (en) * 2020-01-03 2020-05-08 潘自地 Method for preparing thermal expansion microspheres based on interfacial polymerization
CN111315473A (en) * 2017-11-21 2020-06-19 诺力昂化学品国际有限公司 Thermally expandable microspheres prepared from bio-based monomers
CN111647235A (en) * 2019-03-04 2020-09-11 合肥华凌股份有限公司 Novel migration-resistant PVC sealing material and application thereof
CN113549241A (en) * 2020-04-23 2021-10-26 南京工业大学 Polymer foaming microsphere and preparation method thereof
WO2022041978A1 (en) 2020-08-25 2022-03-03 浙江衢州巨塑化工有限公司 Thermally expandable polyvinylidene chloride microsphere and preparation method therefor
US11505687B2 (en) 2020-08-05 2022-11-22 Nano And Advanced Materials Institute Limited Environmentally degradable foamed master batch composition and using thereof

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WO2014036681A1 (en) * 2012-09-04 2014-03-13 西能化工科技(上海)有限公司 Heat-expandable microspheres, preparation method and use thereof
CN104379647B (en) * 2012-09-04 2018-06-05 西能化工科技(上海)有限公司 Heat-expandable microsphere and its preparation and application
CN108770358A (en) * 2015-12-31 2018-11-06 聚合物胶粘剂密封胶系统公司 System and method for the flexible sealing agent with density modifier
CN105693908A (en) * 2016-02-17 2016-06-22 湖南方锐达科技有限公司 Method for wrapping thermal-expandable microspheres again
CN105693908B (en) * 2016-02-17 2017-11-14 湖南方锐达科技有限公司 The preparation method that a kind of hot expended microsphere coats again
CN108699422A (en) * 2016-02-19 2018-10-23 松本油脂制药株式会社 Heat-expandable microsphere and application thereof
US11746204B2 (en) 2016-02-19 2023-09-05 Matsumoto Yushi-Seiyaku Co., Ltd. Heat-expandable microspheres and applications thereof
CN107459671A (en) * 2017-08-22 2017-12-12 成都新柯力化工科技有限公司 A kind of modified expanded microballoon for polypropylene plastics foaming and preparation method thereof
CN107739492A (en) * 2017-09-26 2018-02-27 西能化工科技(上海)有限公司 Light resilient solid tyre and preparation method thereof
CN107915799B (en) * 2017-10-23 2021-01-01 福建省灿辉环保科技有限公司 High-efficiency thermal expansion microsphere and preparation method thereof
CN107915799A (en) * 2017-10-23 2018-04-17 陈晨特 A kind of new and effective microspheres and preparation method thereof
CN111315473A (en) * 2017-11-21 2020-06-19 诺力昂化学品国际有限公司 Thermally expandable microspheres prepared from bio-based monomers
CN111315473B (en) * 2017-11-21 2022-01-11 诺力昂化学品国际有限公司 Thermally expandable microspheres prepared from bio-based monomers
US11208538B2 (en) 2017-11-21 2021-12-28 Nouryon Chemicals International B.V. Thermally expandable microspheres prepared from bio-based monomers
CN108218372B (en) * 2017-12-08 2020-11-10 西能化工科技(上海)有限公司 Ultra-light energy storage gypsum board and preparation method thereof
CN108218372A (en) * 2017-12-08 2018-06-29 西能化工科技(上海)有限公司 Ultralight energy-storage gypsum plate and preparation method thereof
CN108097182A (en) * 2018-01-05 2018-06-01 三明市锦浪新材料科技有限公司 A kind of ultra-fine environment protection thermal expanding microcapsules and preparation method thereof
CN108912384B (en) * 2018-07-20 2021-03-30 西能化工科技(上海)有限公司 Ultrahigh-temperature expandable thermoplastic microspheres and preparation method and application thereof
CN108912384A (en) * 2018-07-20 2018-11-30 西能化工科技(上海)有限公司 Superhigh temperature expandable thermoplastic microspheres and its preparation method and application
CN108912383A (en) * 2018-07-20 2018-11-30 西能化工科技(上海)有限公司 Superhigh temperature expandable thermoplastic microspheres and its application
CN108912383B (en) * 2018-07-20 2020-11-10 西能化工科技(上海)有限公司 Ultrahigh-temperature expandable thermoplastic microspheres and application thereof
CN109749534A (en) * 2019-01-10 2019-05-14 西能化工科技(上海)有限公司 Automobile PVC stone-impact-proof paint and preparation method thereof
CN111647235B (en) * 2019-03-04 2022-04-01 合肥华凌股份有限公司 Novel migration-resistant PVC sealing material and application thereof
CN111647235A (en) * 2019-03-04 2020-09-11 合肥华凌股份有限公司 Novel migration-resistant PVC sealing material and application thereof
CN109970466A (en) * 2019-03-29 2019-07-05 东莞市泰赛特汽车用品科技有限公司 A kind of environmental protection brick face antilubricant and preparation method thereof
CN110698721A (en) * 2019-10-15 2020-01-17 江苏科技大学 Polymethacrylimide thermal expansion microsphere and preparation method thereof
CN111116969B (en) * 2020-01-03 2022-04-01 潘自地 Method for preparing thermal expansion microspheres based on interfacial polymerization
CN111116969A (en) * 2020-01-03 2020-05-08 潘自地 Method for preparing thermal expansion microspheres based on interfacial polymerization
CN113549241A (en) * 2020-04-23 2021-10-26 南京工业大学 Polymer foaming microsphere and preparation method thereof
US11505687B2 (en) 2020-08-05 2022-11-22 Nano And Advanced Materials Institute Limited Environmentally degradable foamed master batch composition and using thereof
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