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CN104194599B - A kind of preparation method of fluororine-carbon coating - Google Patents

A kind of preparation method of fluororine-carbon coating Download PDF

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CN104194599B
CN104194599B CN201410411594.5A CN201410411594A CN104194599B CN 104194599 B CN104194599 B CN 104194599B CN 201410411594 A CN201410411594 A CN 201410411594A CN 104194599 B CN104194599 B CN 104194599B
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fluororine
carbon coating
component
preparation
proportioning
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CN104194599A (en
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林维红
李景菲
周光大
林建华
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Hangzhou Forster applied materials Limited by Share Ltd
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Hangzhou First PV Material Co Ltd
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Abstract

The present invention discloses a kind of preparation method of fluororine-carbon coating, this fluororine-carbon coating is made up of first component and component B, during use, be that 1 ~ 2:1 mix with component B according to the ratio of quality consumption by first component, wherein first component is made up of fluorine carbon base polyurethane prepolymer for use as, nanometer inorganic filler, hydrolysis stabilizer, dispersion agent, flow agent, tin class catalyzer, initiator, vinylformic acid hydroxyl ester, anhydrous diluents; Component B is made up of Hydroxylated acrylic resin, isocyanate curing agent and anhydrous diluents.The present invention effectively can improve crosslinked polymer density in fluororine-carbon coating, makes it to have IPN inierpeneirating network structure more closely.Obtained fluororine-carbon coating, weather-proof, water-fast, chemicals-resistant, salt spray resistance excellence, hardness and wear resisting property are given prominence to, and are a kind of fluororine-carbon coatings that can be used for the excellent property of solar cell backboard.

Description

A kind of preparation method of fluororine-carbon coating
Technical field
The present invention relates to a kind of preparation method of fluororine-carbon coating, belong to material surface resist technology field.
Background technology
Photovoltaic industry, as the important component part of renewable energy source, has become the main method solving global energy crisis.After 2008, the application of solar cell is constantly expanded, from aviation, surface power station to roof, curtain wall, from temperate zone, the torrid zone to high and cold, desert region, become the part in people's life gradually.Riseing of solar cell demand, also determines the generalization of material used for solar batteries, production domesticization.Solar module main raw used, comprises crystal silicon chip, silver slurry, toughened glass, EVA adhesive film, terminal box, backboard.In China's Own Brand, production technique and the quality product of the first five kind material all reach level leading in the world, no longer rely on import.But the quality level of the backboard of domestic production and American-European-Japanese also there is a big difference, also far can not meet the requirement of some harsh and unforgiving environments.
Before 2008, on market, the structure of backboard product mainly contains four kinds, as TPT, TPE, 3A, PET.All based on import, as Isovolta, Madico, Coveme, Honeywell, Krempel, 3M, SFC, Toyal.In the end of the year 2008, in Du Pont under the monopolization of Tedlar fluorine film, holding at high price of backboard, domestic encapsulation company is proposed the higher application type backboard of cost performance.Application type backboard mainly based on domestic independent research, as come in Hangzhou Foster, Suzhou, Suzhou match 5 etc.Application type backboard can not only reach the performance of identical with TPT backboard water-fast, heat-resisting, ultraviolet aging resistance, also has easy production technique, therefore obtains in recent years applying more and more widely.But; by contrast; the anti-blown sand of application type backboard is relatively weak; wear resistance is also less than 30% of TPT type backboard; in the area that some weather is harsh, the Northwest that especially dust storm is large, backboard external coating (EC) drops by dust storm very easily delamination of swiping; thus reduce the provide protection of backboard to assembly, reduce work-ing life and the generating efficiency of solar cell.Therefore, develop a class wear resistance higher, simultaneously water tolerance, alkaline-resisting, solvent resistant, ageing-resistant etc. in all show excellent over-all properties fluororine-carbon coating be the problem that solar cell backboard industry urgently solves.
Summary of the invention
The technical problem to be solved in the present invention is, overcomes deficiency of the prior art, provides a kind of preparation method of fluororine-carbon coating.
For technical solution problem, solution of the present invention is:
A preparation method for fluororine-carbon coating, comprises the following steps:
(1) preparation of first component, comprises following sub-step:
(1.1) first polyester polyol and isocyanate curing agent, the first anhydrous diluents are joined in reactor successively, warming while stirring, treat that temperature rises to 75 DEG C ~ 85 DEG C, add the first tin class catalyzer, react 2 ~ 3 hours; Wherein, the mol ratio of the OH in polyester polyol and the NCO in isocyanate curing agent is 1:3 ~ 4, isocyanate curing agent is equal with the first anhydrous diluents quality, and the quality of the first tin class catalyzer is 0.01 ~ 0.1% of the total mass of polyester polyol, isocyanate curing agent and the first anhydrous diluents;
(1.2) in the reaction system of step (1.1), fluorocarbon resin is added, mix rear continuation reaction 2 ~ 3 hours, obtain fluorine carbon base polyurethane prepolymer for use as, wherein, in the polyester polyol added in the hydroxyl moles in fluorocarbon resin and step 1.1, hydroxyl moles ratio is 7 ~ 9:1;
(1.3) fluorine carbon base polyurethane prepolymer for use as step 1.2 obtained is poured high-speed mixer into and is stirred, after being cooled to room temperature, in fluorine carbon polyurethane prepolymer weight, take the nano sized inorganic fillers of 10 ~ 15%, 3 ~ 5% hydrolysis stabilizers, the dispersion agent of 1 ~ 5%, the flow agent of 0.1 ~ 1%, 0.1 ~ 1% the second tin class catalyzer, 0.01 ~ 0.1% initiator, 5 ~ 10% vinylformic acid hydroxyl esters, 50 ~ 100% the second anhydrous diluents, join successively in high-speed mixer, keep rotating speed 3000 revs/min, mix 1 ~ 2 hour, make first component, deposit in dry sealed vessel stand-by,
(2) preparation of component B: first Hydroxylated acrylic resin and isocyanate curing agent, the 3rd anhydrous diluents are joined in reactor successively, slowly heat up while stirring, treat that temperature rises to 75 DEG C ~ 85 DEG C, add the 3rd tin class catalyzer, continue reaction after 2 ~ 3 hours, slowly cool to room temperature, make component B, deposit in dry sealed vessel stand-by, OH mole number in Hydroxylated acrylic resin is 1:3 ~ 4 with the ratio of NCO mole number in isocyanate curing agent, and isocyanate curing agent is equal with the quality of the 3rd anhydrous diluents; The quality of the 3rd tin class catalyzer is 0.01 ~ 0.1% of the total mass of Hydroxylated acrylic resin, isocyanate curing agent and the 3rd anhydrous diluents;
(3), when using, be that 1 ~ 2:1 mix with component B according to the ratio of quality consumption by first component, be evenly coated in by adhesive material surperficial, coating dry film thickness is 20 ~ 25 microns, and solidification value is 120 DEG C ~ 175 DEG C, and set time is 1 ~ 5min.
Described polyester polyol is made up of according to any proportioning one or more in aromatic polyester polyol, polycarbonate polyol.
Described isocyanate curing agent is made up of according to any proportioning one or more in hexamethylene diisocyanate trimer, hexamethylene diisocyanate affixture, isophorone diisocyanate trimer, isophorone diisocyanate affixture, hydrogenation of benzene dimethylene diisocyanate tripolymer, hydrogenation of benzene dimethylene diisocyanate affixture.
Described fluorocarbon resin is be made up of according to any proportioning one or more in vinylidene type fluorocarbon resin, three fluorine-type fluorocarbon resins, four fluorine-type fluorocarbon resins; As preferably, the hydroxyl value of fluorocarbon resin is 50 ~ 60mgKOH/g, and Oil repellent is 26% ~ 30%.
Described nano sized inorganic fillers is made up of according to any proportioning one or more in nano silicon, nanometer silicon carbide, nano aluminium oxide, nano titanium oxide, nm-class boron nitride, nano barium sulfate, nano-calcium carbonate, nanometer Magnesium Silicate q-agent, nano-sized iron oxide.
Described hydrolysis stabilizer is made up of according to any proportioning one or more in monomer Carbodiimides hydrolysis stabilizer, polycarbodiimide class hydrolysis stabilizer, monocarboxylic Racemic glycidol hydrolysis of lipid stablizer.
Described dispersion agent is by containing the segmented copolymer class dispersion agent of pigment affinity groups, acrylic block copolymers class dispersion agent, height branched structure polyester dispersion agent, form according to any proportioning containing one or more in acid group copolymer analog dispersion agent, hydroxy functional group carboxylic acid esters dispersion agent.
Described flow agent is made up of according to any proportioning one or more in polyether siloxane copolymer class flow agent, reactive polyether modified fluoro-silicone oxygen alkanes flow agent, polyether-modified poly organo siloxane flow agent, polyacrylate(s) flow agent.
The first described tin class catalyzer, the second tin class catalyzer and the 3rd tin class catalyzer are made up of according to any proportioning one or both in monobutyltin oxide, monobutyl three isocaprylic acid tin;
Described initiator is made up of according to any proportioning one or more in cyclohexanone peroxide, dibenzoyl peroxide, tertbutyl peroxide, Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile);
Described vinylformic acid hydroxyl ester is made up of according to any proportioning one or more in Hydroxyethyl acrylate, Propylene glycol monoacrylate, hy-droxybutyl, hydroxyethyl methylacrylate, Rocryl 410, methacrylate;
Described thinner 1, thinner 2 and thinner 3 are made up of according to any proportioning one or more in ethyl acetate, butylacetate, acetone, positive butanone, 1-Methoxy-2-propyl acetate, glycol methyl ether acetate, dimethylbenzene.
An application for fluororine-carbon coating, is characterized in that, this is applied as by fluororine-carbon coating for being coated in basilar membrane, makes application type solar cell backboard; Described basilar membrane is selected from PET substrate's film, polybutylene terephthalate basilar membrane, PEN basilar membrane, PBN basilar membrane, poly-11 lactam group counterdies, nylon 12 basilar membrane, polypropylene-base counterdie, polyvinyl counterdie, toughened glass.
Beneficial effect of the present invention is mainly reflected in:
The present invention adopts the means of Polymer Synthesizing, carries out total innovation from the preparation method of the preparation method of host preparation method and chemical structure, solidifying agent and chemical structure, coating and chemical structure.Compared with the preparation method of existing dual coating type backboard fluororine-carbon coating, technique effect of the present invention is: fluororine-carbon coating internal structure can be made to form effective IPN inierpeneirating network structure, and the strengthening action of effectively combining nano mineral filler, cause fluororine-carbon coating to have excellent ageing resistance, hardness and wear resistance, expand the range of application of dual coating type backboard.
Embodiment
Below in conjunction with embodiment, the invention will be further described, but protection scope of the present invention is not only confined to embodiment.
It should be noted that, the property indices of fluororine-carbon coating is undertaken measuring by following method:
1. coating hardness
Testing method reference standard GB/T6739 " hardness of film pencil assay method ".
Sample making: be that 1 ~ 2:1 mixes with component B according to the ratio of quality consumption by first component, by automatization, continuously shaped or batch process is evenly coated in material surface, coating dry film thickness is 5 ~ 30 microns, and solidification value is 120 DEG C ~ 175 DEG C, and set time is 1 ~ 5min.
Pencil is moved horizontally 3mm with 0.5mm/s speed on sample and measures hardness, according to cut, record hardness values.
2. coating wear resistance
Testing method reference standard GB/T23988 " coating wear resistance measures knockout method ".
Sample making: be that 1 ~ 2:1 mixes with component B according to the ratio of quality consumption by first component, by automatization, continuously shaped or batch process is evenly coated in material surface, coating dry film thickness is 20 ~ 25 microns, and solidification value is 120 DEG C ~ 175 DEG C, and set time is 1 ~ 5min.
Standard sand is highly fallen the sample of 45° angle from 914mm, according to eroded area, calculates knockout amount.
3. constant wet and heat ageing resistant performance
Hydrothermal aging test is carried out by GB/T2423.3 test method.
Test conditions :+85 DEG C, relative humidity 85%.
Test and forward and backward sample yellowness index (Δ YI) to be measured by GB GB2409 " plastics yellowness index test method ".
Embodiment 1
A kind of fluororine-carbon coating, is made up of first and second liang of components.
Prepared by first component: by 1000g (5.18molOH group) aromatic polyester polyol 121E(Nippon Polyurethane Industry Co., Ltd.), 3330g (15.54molNCO group) hexamethylene diisocyanate trimer solidifying agent HT-90BS(Wanhua Chemical Group Co., Ltd.), 3330g anhydrous acetic acid butyl ester (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 80 DEG C, add the monobutyl three isocaprylic acid tin catalyst (Jin Tian raw material company limited) of 7.6g, react 2.5 hours, 37744g (40.44molOH group) fluorocarbon resin SW-5570(Shanghai Sheng Wei trade Co., Ltd is added again in reaction system), mix and continue reaction after 2.5 hours, pour reaction mixture into high-speed mixer while hot, after being slowly chilled to room temperature, take 4542g nano silicon A380(Germany Degussa), chemical research institute of 1365g haplotype Carbodiimides hydrolysis stabilizer SW-100(Shanxi Province), 455g is containing Bi Ke chemical company of acid group copolymer analog dispersant B YK9076(Germany), Wei Bo Chemical Co., Ltd. of 228g polyether-modified poly organo siloxane flow agent 505(Shenzhen), 45.5g monobutyltin oxide catalyzer (Shinning company limited of Taixing City), 4.9g cyclohexanone peroxide initiator (Lanzhou auxiliary reagent factory), 2275g Hydroxyethyl acrylate (auspicious industry is gathered in Shanghai), 27250g anhydrous propylene glycol methyl ether acetate thinner (Zhejiang chemical company) joins in high-speed mixer successively, keep 3000 revs/min, mix 1.5 hours, make first component, deposit in dry sealed can stand-by,
Prepared by component B: first by 1000g (2.61molOH group) the great people in Hydroxylated acrylic resin HU57042(Shanghai), the D120N(Mitsui Chemicals, Inc of 3813g (10.44molNCO group) hydrogenation of benzene dimethylene diisocyanate affixture solidifying agent), 3813g anhydrous acetic acid butyl ester (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 75 DEG C, add 8.6g monobutyl three isocaprylic acid tin catalyst (Jin Tian raw material company limited), continue reaction after 3 hours, slowly cool to room temperature, make component B, deposit in dry sealed can stand-by,
Prepared by application type solar cell backboard: be the mixing of 1:1 with component B according to the ratio of quality consumption by first component, by automatization, the continuously shaped or even dual coating of batch process is at pet film material surface, coating dry film thickness is 20 microns, solidification value is 120 DEG C, and set time is 5min.
Embodiment 2
A kind of fluororine-carbon coating, is made up of first and second liang of components.
Prepared by first component: by 1000g (2.36molOH group) aromatic polyester polyol AK3080(Foshan with moral Chemical Co., Ltd.), 3332g (9.44molNCO group) isophorone diisocyanate trimer Z4470BA(Bayer Bitterfeld GmbH), 3332g anhydrous ethyl acetate (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 75 DEG C, add the monobutyltin oxide (Shinning company limited of Taixing City) of 7.6g, react 3 hours, 19824g (21.24molOH group) fluorocarbon resin GK570(Daikin is added again in reaction system), mix and continue reaction after 3 hours, pour reaction mixture into high-speed mixer while hot, after being slowly chilled to room temperature, take 4124g nano aluminium oxide TBD-L30(Wuxi and open up titanium white Products Co., Ltd of BDCom), 1376g monomer Carbodiimides hydrolysis stabilizer Ipowder(Lay mattress chemistry), Bi Ke chemical company of 550g height branched structure polyester dispersant B YK2151(Germany), EFKA auxiliary agent company of 274g polyacrylate(s) flow agent IRGAFLOW110(Holland), 274g monobutyltin oxide catalyzer (Shinning company limited of Taixing City), 26g tertbutyl peroxide initiator (Lanzhou auxiliary reagent factory), 1375g hy-droxybutyl (auspicious industry is gathered in Shanghai), the anhydrous glycol methyl ether acetate thinner of 27490g (Zhejiang chemical company) joins in high-speed mixer successively, keep 3000 revs/min, mix 1 hour, make first component, deposit in dry sealed can stand-by,
Prepared by component B: first by 1000g (2.5molOH group) Hydroxylated acrylic resin 7331(Changxing chemistry), 2972g (7.5molNCO group) isophorone diisocyanate affixture solidifying agent D140(Mitsui Chemicals, Inc), 2972g anhydrous ethyl acetate (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 80 DEG C, add 6.8g monobutyltin oxide catalyzer (Shinning company limited of Taixing City), continue reaction after 2.5 hours, slowly cool to room temperature, make component B, deposit in dry sealed can stand-by,
Prepared by application type solar cell backboard: be the mixing of 1.3:1 with component B according to the ratio of quality consumption by first component, by automatization, the continuously shaped or even dual coating of batch process is on toughened glass surface, coating dry film thickness is 20 microns, solidification value is 160 DEG C, and set time is 2min.
Embodiment 3
A kind of fluororine-carbon coating, is made up of first and second liang of components.
Prepared by first component: by 1000g (2.19molOH group) polycarbonate polyol PC-61(Nippon Polyurethane Industry Co., Ltd.), 1483g (7.66molNCO group) hexamethylene diisocyanate trimer solidifying agent TKA100(Asahi Chemical Corp), the anhydrous positive butanone of 1483g (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 80 DEG C, add the monobutyl three isocaprylic acid tin catalyst (Shinning company limited of Taixing City) of 0.4g, react 2 hours, 15094g (17.52molOH group) fluorocarbon resin L101(Huambo painting company limited is added again in reaction system), mix and continue reaction after 3 hours, pour reaction mixture into high-speed mixer while hot, after being slowly chilled to room temperature, take 1144g nanometer carbon black JY-101P(Hangzhou monarch one novel material company limited), 1716g nano titanium oxide TR81(U.S. Hensel is graceful), 763g polycarbodiimide class hydrolysis stabilizer P200(Lay mattress chemistry), Bi Ke chemical company of 953g acrylic block copolymers class dispersant B YK116(Germany), 20g reactive polyether modified fluoro-silicone oxygen alkanes flow agent BD-3350(Hangzhou Bao Er get organosilicon company limited), 95g monobutyl three isocaprylic acid tin catalyst (the far and near Chemical Co., Ltd. in Nantong), 9.6g Diisopropyl azodicarboxylate initiator (Lanzhou auxiliary reagent factory), 1906g Rocryl 410 (German Degussa), 15248g anhydrous propylene glycol methyl ether acetate thinner (Zhejiang chemical company) joins in high-speed mixer successively, keep 3000 revs/min, mix 1 hour, make first component, deposit in dry sealed can stand-by,
Prepared by component B: first by 1000g (1.65molOH group) Hydroxylated acrylic resin 575X(Bayer Bitterfeld GmbH), 1517g (5.78molNCO group) hexamethylene diisocyanate affixture solidifying agent HXT(Nippon Polyurethane Industry Co., Ltd.), the anhydrous positive butanone of 1517g (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 85 DEG C, add 0.5g monobutyl three isocaprylic acid tin catalyst (Shinning company limited of Taixing City), continue reaction after 2 hours, slowly cool to room temperature, make component B, deposit in dry sealed can stand-by,
Prepared by application type solar cell backboard: be the mixing of 2:1 with component B according to the ratio of quality consumption by first component, by automatization, the continuously shaped or even dual coating of batch process is at nylon 12 thin-film material surface, coating dry film thickness is 25 microns, solidification value is 175 DEG C, and set time is 1min.
Embodiment 4
A kind of fluororine-carbon coating, is made up of first and second liang of components.
Prepared by first component: by 1000g (5.62molOH group) polyester polyol PS-3152(Jinan Hai Hao Chemical Co., Ltd.), 6149g (17.42molNCO group) isophorone diisocyanate trimer Z4470BA(Bayer Bitterfeld GmbH), 6149g anhydrous dimethyl benzene (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 75 DEG C, add the monobutyltin oxide catalyzer (the far and near Chemical Co., Ltd. in Nantong) of 66g, react 2.5 hours, 48646g (47.78molOH group) fluorocarbon resin ZHM-2(east fluorine chemical is added again in reaction system), mix and continue reaction after 3 hours, pour reaction mixture into high-speed mixer while hot, after being slowly chilled to room temperature, take 620g nano silicon JRNG41(Xuancheng Jingrui New Material Co., Ltd.), 5581g nano titanium oxide TR81(U.S. Hensel is graceful), 3100g bisphenol A diglycidyl ether hydrolysis stabilizer (Zhengzhou Nuo Kang medicine intermediate company limited), 1860g is containing the Bi Ke chemical company of segmented copolymer class dispersant B YK2155(Germany of pigment affinity groups), 310g polyether siloxane copolymer class flow agent Tego-432(Germany enlightening is high), 490g monobutyl three isocaprylic acid tin catalyst (the far and near Chemical Co., Ltd. in Nantong), 49g dibenzoyl peroxide initiator (Lanzhou auxiliary reagent factory), 4900g hydroxyethyl methylacrylate (German Degussa), 31005g anhydrous dimethyl benzene (Zhejiang chemical company) thinner joins in high-speed mixer successively, keep 3000 revs/min, mix 2 hours, make first component, deposit in dry sealed can stand-by,
Prepared by component B: first by 1000g (2.38molOH group) Hydroxylated acrylic resin Setalux1901(Niu Peisi industrial group), 2189g (8.34molNCO group) hexamethylene diisocyanate affixture solidifying agent HXT(Nippon Polyurethane Industry Co., Ltd.), 2189g anhydrous dimethyl benzene (Zhejiang chemical company) joins in reactor successively, slowly heat up while stirring, treat that temperature appreciates 75 DEG C, add 2.6g monobutyltin oxide catalyzer (the far and near Chemical Co., Ltd. in Nantong), continue reaction after 3 hours, slowly cool to room temperature, make component B, deposit in dry sealed can stand-by,
Prepared by application type solar cell backboard: be the mixing of 1.6:1 with component B according to the ratio of quality consumption by first component, by automatization, the continuously shaped or even dual coating of batch process is at polybutylene terephthalate thin-film material surface, coating dry film thickness is 20 microns, solidification value is 150 DEG C, and set time is 3min.
Comparative example 1:
Market is buied TPT type backboard (Korea S), structure is Tedlar+PET+Tedlar, and fluorine film thickness is 25 microns.
Comparative example 2:
Market is buied application type backboard (domestic), structure is fluororine-carbon coating+PET+ fluororine-carbon coating, fluororine-carbon coating thickness 25 microns.
The dual coating type backboard obtained to embodiment 1,2,3,4 and the material of comparative example 1,2 carry out Performance Detection, and result is as shown in table 1.
The performance perameter of the sizing agent that table 1 is obtained
Performance perameter Embodiment 1 Embodiment 2 Embodiment 3 Embodiment 4 Comparative example 1 Comparative example 2
Outward appearance White White Black White White White
Hardness 3H 4H 4H 4H 2H 2H
Knockout volume (L) 400 330 358 430 308 62
Steady damp heat aging examination 3000h yellowness index (Δ YI) 2.5 2.3 1.0 3.0 4.0 5.6
Steady damp heat aging examination 3000h outward appearance Without cracking, bubble-free, without efflorescence Without cracking, bubble-free, without efflorescence Without cracking, bubble-free, without efflorescence Without cracking, bubble-free, without efflorescence Without cracking, bubble-free, without efflorescence Without cracking, bubble-free, without efflorescence
From data in table, a kind of fluororine-carbon coating of the present invention, has excellent ageing-resistant performance, for making application type solar cell backboard, solving the problem that application type backboard hardness is low, wear no resistance, is a kind of excellent fluororine-carbon coating that can be used for application type solar cell backboard.

Claims (10)

1. a preparation method for fluororine-carbon coating, is characterized in that, comprises the following steps:
(1) preparation of first component, comprises following sub-step:
(1.1) first polyester polyol and isocyanate curing agent, the first anhydrous diluents are joined in reactor successively, warming while stirring, treat that temperature rises to 75 DEG C ~ 85 DEG C, add the first tin class catalyzer, react 2 ~ 3 hours; Wherein, the mol ratio of the OH in polyester polyol and the NCO in isocyanate curing agent is 1:3 ~ 4, isocyanate curing agent is equal with the first anhydrous diluents quality, and the quality of the first tin class catalyzer is 0.01 ~ 0.1% of the total mass of polyester polyol, isocyanate curing agent and the first anhydrous diluents;
(1.2) in the reaction system of step (1.1), fluorocarbon resin is added, mix rear continuation reaction 2 ~ 3 hours, obtain fluorine carbon base polyurethane prepolymer for use as, wherein, in the polyester polyol added in the hydroxyl moles in fluorocarbon resin and step (1.1), hydroxyl moles ratio is 7 ~ 9:1;
(1.3) pour the fluorine carbon base polyurethane prepolymer for use as that step (1.2) obtains into high-speed mixer to stir, after being cooled to room temperature, in fluorine carbon polyurethane prepolymer weight, take the nano sized inorganic fillers of 10 ~ 15%, 3 ~ 5% hydrolysis stabilizers, the dispersion agent of 1 ~ 5%, the flow agent of 0.1 ~ 1%, 0.1 ~ 1% the second tin class catalyzer, 0.01 ~ 0.1% initiator, 5 ~ 10% vinylformic acid hydroxyl esters, 50 ~ 100% the second anhydrous diluents, join successively in high-speed mixer, keep rotating speed 3000 revs/min, mix 1 ~ 2 hour, make first component, deposit in dry sealed vessel stand-by,
(2) preparation of component B: first Hydroxylated acrylic resin and isocyanate curing agent, the 3rd anhydrous diluents are joined in reactor successively, slowly heat up while stirring, treat that temperature rises to 75 DEG C ~ 85 DEG C, add the 3rd tin class catalyzer, continue reaction after 2 ~ 3 hours, slowly cool to room temperature, make component B, deposit in dry sealed vessel stand-by, OH mole number in Hydroxylated acrylic resin is 1:3 ~ 4 with the ratio of NCO mole number in isocyanate curing agent, and isocyanate curing agent is equal with the quality of the 3rd anhydrous diluents; The quality of the 3rd tin class catalyzer is 0.01 ~ 0.1% of the total mass of Hydroxylated acrylic resin, isocyanate curing agent and the 3rd anhydrous diluents;
(3), when using, be that 1 ~ 2:1 mix with component B according to the ratio of quality consumption by first component, be evenly coated in by adhesive material surperficial, coating dry film thickness is 20 ~ 25 microns, and solidification value is 120 DEG C ~ 175 DEG C, and set time is 1 ~ 5min.
2. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, is characterized in that, described polyester polyol is made up of according to any proportioning one or more in aromatic polyester polyol, polycarbonate polyol.
3. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, it is characterized in that, described isocyanate curing agent is made up of according to any proportioning one or more in hexamethylene diisocyanate trimer, hexamethylene diisocyanate affixture, isophorone diisocyanate trimer, isophorone diisocyanate affixture, hydrogenation of benzene dimethylene diisocyanate tripolymer, hydrogenation of benzene dimethylene diisocyanate affixture.
4. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, is characterized in that, described fluorocarbon resin is be made up of according to any proportioning one or more in vinylidene type fluorocarbon resin, three fluorine-type fluorocarbon resins, four fluorine-type fluorocarbon resins; The hydroxyl value of fluorocarbon resin is 50 ~ 60mgKOH/g, and Oil repellent is 26% ~ 30%.
5. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, it is characterized in that, described nano sized inorganic fillers is made up of according to any proportioning one or more in nano silicon, nanometer silicon carbide, nano aluminium oxide, nano titanium oxide, nm-class boron nitride, nano barium sulfate, nano-calcium carbonate, nanometer Magnesium Silicate q-agent, nano-sized iron oxide.
6. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, it is characterized in that, described hydrolysis stabilizer is made up of according to any proportioning one or more in monomer Carbodiimides hydrolysis stabilizer, polycarbodiimide class hydrolysis stabilizer, monocarboxylic glycidyl ester class hydrolysis stabilizer.
7. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, it is characterized in that, described dispersion agent by containing pigment affinity groups segmented copolymer class dispersion agent, height branched structure polyester dispersion agent, form according to any proportioning containing one or more in acidic-group copolymer analog dispersion agent, hydroxy functional group carboxylic acid esters dispersion agent.
8. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, it is characterized in that, described flow agent is made up of according to any proportioning one or more in polyether siloxane copolymer class flow agent, reactive polyether modified fluoro-silicone oxygen alkanes flow agent, polyacrylate(s) flow agent.
9. the preparation method of a kind of fluororine-carbon coating as claimed in claim 1, it is characterized in that, the first described tin class catalyzer, the second tin class catalyzer and the 3rd tin class catalyzer are made up of according to any proportioning one or both in monobutyltin oxide, monobutyl three isocaprylic acid tin;
Described initiator is made up of according to any proportioning one or more in cyclohexanone peroxide, dibenzoyl peroxide, tertbutyl peroxide, Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile);
Described vinylformic acid hydroxyl ester is made up of according to any proportioning one or more in Hydroxyethyl acrylate, Propylene glycol monoacrylate, hy-droxybutyl, hydroxyethyl methylacrylate, Rocryl 410, methacrylate;
Described thinner 1, thinner 2 and thinner 3 are made up of according to any proportioning one or more in ethyl acetate, butylacetate, acetone, positive butanone, 1-Methoxy-2-propyl acetate, glycol methyl ether acetate, dimethylbenzene.
10. an application for fluororine-carbon coating according to claim 1, is characterized in that, this is applied as by fluororine-carbon coating for being coated in basilar membrane, makes application type solar cell backboard; Described basilar membrane is selected from PET substrate's film, polybutylene terephthalate basilar membrane, PEN basilar membrane, PBN basilar membrane, poly-11 lactam group counterdies, nylon 12 basilar membrane, polypropylene-base counterdie, polyvinyl counterdie, toughened glass.
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