CN1244556A - Fluoric copolymer paint with PTFE as main component and its preparation - Google Patents
Fluoric copolymer paint with PTFE as main component and its preparation Download PDFInfo
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- CN1244556A CN1244556A CN 99113196 CN99113196A CN1244556A CN 1244556 A CN1244556 A CN 1244556A CN 99113196 CN99113196 CN 99113196 CN 99113196 A CN99113196 A CN 99113196A CN 1244556 A CN1244556 A CN 1244556A
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Abstract
The fluoric copolymer paint is prepared through copolymerization of four kinds of monomers, including tetrafluoroethylene, aliphatic ester with perhaps isomerized olefine, fatty enol and/or enol dihydric alcohol ether, alphatic olefine acid in solvent, and in the presence of initiator. Compared with available technology, the paint has the features of high fluoride content, high solid content, good humidification to pigment, excellent dispersivity, etc. and the paint film produced has high hardness, high flexiblity, strong adhesion, high shock resistance, excellent salt-fog resistance, excellent chemical resistance and high weatherability.
Description
The invention belongs to fluorinated copolymer paint field, particularly tetrafluoroethylene and the copolymerization of a plurality of unsaturated fatty acids compounds of group forms polymer coating.
Fluoropolymer has favorable mechanical performance and excellent chemical proofing, weathering resistance, this be the C-F key that has owing to fluoropolymer can be from being situated between than due to the reasons such as c h bond is much bigger.
But fluoropolymer mostly has higher degree of crystallinity, thereby is difficult to be dissolved in the solvent.Can be dissolved in the solvent be the key that is made into solvent based coating.With monomer with relevant functional group and fluorochemical monomer copolymerization, then in the fluoropolymer molecular chain because of having the segment that can be dissolved in solvent, the degree of crystallinity of whole fluoropolymer is reduced, just can be mixed with solvent based coating, be referred to as fluoro-containing coating, for solving the crosslinking curing of fluoro-containing coating, again in the macromole of multipolymer, introduced the functional group of hydroxyl, at when construction and the linking agent that adds crosslinking curing at normal temperatures.The existing report of this kind method relevant patent at home and abroad.
Be du pont company the earliest, develop based on vinylidene fluoride, with the random copolymers of tetrafluoroethylene and vinyl butyrate in 1970's.This multipolymer dissolves in methylethylketone, uses up or electron rays irradiation is carried out crosslinked.Its shortcoming be construction time and radiation exposure less than local crosslinked insufficient, and influenced the quality of fluorine coating.
At the end of the eighties, Japan AGC Co., Ltd. develops with trifluorochloroethylene, vinyl fatty ester, has the terpolymer fluorine coating (the clear 61-57609 of TOHKEMY) of the vinyl ether of hydroxyl, is to form paint film by chemically crosslinked.For example: the A101-B fluorine coating of the said firm, because be by chemically crosslinked, application property goes a step further than E.I.Du Pont Company, but the post-treatment of making when coating with lacquer is poor, promptly wetting insufficient with colo(u)rant dispersion, easily produces lacquer diseases such as loose colour.
Chinese patent CN1145386A is by the quarternary copolymerized carboxyl functional group of having introduced based on trifluorochloroethylene, solved fluorine coating make when lacquer the colo(u)rant dispersion wettability poor, easily produce shortcoming such as lacquer disease, but produce the deficiency of anti-alcohols poor performance.
And all emphasize in the patents such as the French CN1046912A of Atochem (FR) Cedex 22, 94091 Paris La Defense, France, CN1046911A, CN1060850A, CN1060849A: the fluorochemical monomer segment is by selecting another kind of fluorochemical monomer in conjunction with obtaining at least two kinds of monomeric mixtures in vinylidene fluoride and tetrafluoroethylene, trifluorochloroethylene, R 1216 or the three kinds of monomers.Rather than to adopt single fluorochemical monomer, major cause be the solution solvability that does not have fine solution fluorochemical monomer multipolymer.Promptly can better not reduce the degree of crystallinity of multipolymer, make it to be soluble in the solvent.And the solids content of multipolymer low (15-45%) difference of hardness, gloss are low.
In addition, Japanese kokai publication hei 10-101739 patent has been emphasized fluo-copolymer, dissolves in scentlessly not contain in the petroleum solvent series of aromatics, with compliance with environmental protection requirements.The hydrofluoric ether of patent is: trifluorochloroethylene, tetrafluoroethylene, trifluoro-ethylene, vinylidene, vinyl fluoride, R 1216, hexafluoro-isobutene etc., and add-on is 20～47 moles of % of monomer total amount; Surpass 47 moles of molten Jie's property step-downs of %.Because multipolymer fluorine content is low, thus this patent in weathering resistance, the erosion resistance aspect is not best.
At the defective that above prior art exists, the present invention aims to provide a kind of high fluorine content, high solids content, and solvent is had good solvability, and the fluorinated copolymer coating that good corrosion-resistant agent, weathering resistance are arranged.
The present invention is in order better to bring into play the weathering resistance of fluo-copolymer, the natural characteristics that erosion resistance is former fluoro-resin, and hydrofluoric ether adopts single tetrafluoroethylene (TFE) monomer.Can improve the fluorine content of multipolymer.
For example:
CH
2=CHF (VF) fluorine content 41.3%
CF
2=CFCl (CTFE) fluorine content 48.9%
CH
2=CF
2(VDF) fluorine content 59.4%
CF
2=CF
2(TFE) fluorine content 76.0%
Be that the fluorine content of TFE is for the highest in the hydrofluoric ether of identical mole.
In order effectively to reduce the degree of crystallinity of multipolymer, when selecting vinyl compound, adopt vinyl ester and isomery vinyl compound and usefulness, purpose is during with the TFE copolymerization, the vinyl segment can relatively be evenly distributed on the macromole long-chain, gives uniform molten Jie's property.
Equally, cross-linking density is even when making multipolymer crosslinked at normal temperatures, the i.e. OH base functional group of cross-linking set is provided, adopt the vinyl ether of hydroxyl, the allylic cpd and the usefulness of hydroxyl, when making with the TFE copolymerization, reactivity ratio and TFE are complementary, and make that hydroxyl can distribute more uniformly on the copolymer molecule chain.
The present invention carries out the multi-component copolymer reaction with following four kinds of relevant monomers.CF
2＝CF
2???????????????????????????????????????????????????A
CH
2＝CH-R
5-OH????????????????????????????????C
1
CCH
2=CH-R
6-O-R
7-OH C
2 R wherein
1The normal chain alkyl of=carbon number 1～5;
R
2＝(CH
2)n
1，n＝0～2；
R
3The normal chain alkyl of=carbon number 1～2;
R
4The normal chain alkyl of=carbon number 1～2;
R
5＝(CH
2)n
2，n
2＝1～4；
R
6＝(CH
2)n
3，n
3＝0～2；
R
7＝(CH
2)n
4，n
4＝2～6；
R
8=(CH
2) n
5, n
5=0～8; The molar percentage that four kinds of monomers participate in reaction is:
A∶B∶C∶D∶(50.0～55.0)∶(35.0～42.0)∶(6.0～7.5)∶(0.5～4.0)
In the monomers B, B
1Can use separately; The present invention emphasizes B
1And B
2While and usefulness, it is time spent mol ratio B also
1: B
2=1.0: (2～1).
C is provided among the monomer C of hydroxyl
1, C
2Can use separately; The present invention emphasizes C
1And C
2While and usefulness, it is time spent mol ratio C also
1: C
2=1: (2.5～1).
Polymerization technique is to adopt solution method quarternary copolymerized.Solvent is the mixed solvent of aliphatics ketone (methylethylketone, methyl iso-butyl ketone (MIBK) etc.) acetates (vinyl acetic monomer, N-BUTYL ACETATE etc.); Proportioning is a ketone: acetates=(60～50): (40～50), consumption are 30～45% of reaction monomers total amount amount.Initiator is azo-compound or acyl peroxide compound etc., and consumption is 1～3% of a reaction monomers gross weight.
In the 2L autoclave, add mixed solvent and remove A, B
2Outer other monomer, and add initiator.Under 0 ℃ of decompression (750mmHg post), add A, B
2, open the autoclave stirring arm, heat up.Temperature of reaction is controlled at 68～78 ℃, and it is 2.0～2.8MPa that reaction pressure begins, and reaction end of a period pressure all is about 0.8～1.0MPa.Reaction times is about 20～22h.
The chain-like structure synoptic diagram of the resulting multipolymer of copolymerization is:
R wherein
1=carbon number is 1～5 normal chain alkyl;
R
2＝(CH
2)n
1，n
1＝0～2；
R
3=carbon number is 1～2 normal chain alkyl;
R
4=carbon number is 1～2 normal chain alkyl;
R
5＝(CH
2)n
2，n
2＝1～4；
R
6＝(CH
2)n
3，n
3＝0～2；
R
7＝(CH
2)n
4，n
4＝2～6；
R
8＝(CH
2)n
5，n
5＝0～8；
Four big components shared molar percentage in polymkeric substance is: A: B: C: D=(50.0～55.0): (35.0～42.0): (6.0～7.5): (0.5～4.0).
The present invention adopts vinyl ester can reduce the degree of crystallinity of fluoropolymer, make it better to be dissolved in the solvent, but vinyl ester segment Yishui River Jie in order to overcome this defective, adopts vinyl ester and vinyl compound also with being of the present invention one big characteristics.Selected vinyl compound is the isomerized vinyl compound of alkyl.To improve the multipolymer second-order transition temperature, increase hardness of paint film, improve water-fast erosion.
The oxy-compound that the present invention introduces is enol, diols alkenyl ether, or both and usefulness.Because oxy-compound is except that providing cross-linking set, also directly influence some other rerum natura of paint films such as sticking power.Both and usefulness all can have oxy-compound and TFE monomer copolymerizable in the different time sections of copolymerization.Thereby the distribution of hydroxyl on macromolecular chain segment be tending towards evenly, when carrying out crosslinking curing with linking agent, can guarantee that cross-linking density is than homogeneous.So, just can improve the anti-alcohol of paint film widely, performances such as anti-ketone.The rerum natura of gained multipolymer is: hydroxyl value 80～92mgKOH/g acid number 5.8～8.5mgKOH/g; Solid content 52～62%; Proportion 1.040～1.060; Viscosity (being coated with-4 glasss) 80～120s is faint yellow transparent thick liquid.
Compared with prior art, the advantage that the present invention gives prominence to is: (1) high solids content, Japan AGC product only are 48～50%, and (2) can be fine wetting with pigment, disperse can prevent the sick generations of lacquer such as loose colour easily.(3) multipolymer paint film property excellence: 1. hardness height, pendulum-rocker hardness reaches 0.83～0.85, and the Japan AGC product only is 0.7; 2. flexibility reaches below the 2mm, and the paint film model is folding, and the paint film that base material fractures does not chap; 3. gloss is 68～70%, and is better than French atropic company product; 4. good (method of drawing a circle is 1 grade to sticking power, and shock-resistant is 50cm.(4) salt fog resistance is good, and 3000h is 1 grade.(5) chemical resistance is good: 1. the paint film coupon is at 10% HCl, 10%H
2SO
4, soak two months no changes among the 10%NaOH; 2. in dehydrated alcohol, soak a month no change, 3. clean paint film＞100 time, be better than the index of CN1145386A with acetone.(6) good weatherability, artificial accelerated aging 3000h, the loss of gloss rate is 5～11%, is better than the above prior art products.
Following embodiment illustrates the present invention, but does not limit the embodiment of the invention 1～6.
(1) embodiment 1～6 equipment used and technology
Adopt the reactor that 2L has induction stirring, be provided with cooling coil in the still, the still outer wall is with electric heater unit.
According to listed embodiment 1～6 each component feeding quantity of table 1, feed in raw material.Order of addition(of ingredients) is 2. B of 1. mixed solvent
1, 3. initiator of C, D; After, logical chilled brine in still internal cooling coiled pipe when still internal cooling to 0 ℃, vacuumizes and (750mmHg), fills N
2Gas vacuumizes once more; After, rely on B
2If (use B
2The time) and the pressure of A own, if use B
2The time add B earlier
2After add A.
Open and stir and intensification.Polymerization temperature is controlled at 68～70 ℃.Polymerization initiation pressure 2.0～2.8MPa, polymerization end of a period pressure is 0.8～1.0MPa.Polymerization time is 20～22h.
(2), the add-on of embodiment 1～6 each component
The add-on of each component sees Table 1.
The add-on of table 1 embodiment 1～6 each component
(3) embodiment 1～6 resulting multipolymer characteristic
| Component | Monomer | Embodiment | ||||||
| ????1 | ????2 | ????3 | ????4 | ????5 | ????6 | |||
| ??A | Tetrafluoroethylene | ???360 | ???400 | ????300 | ????360 | ???360 | ????380 | |
| ??B | ??B1 | The vinyl acetate allyl bexanoate | ???86 | ???86 | ????206 | ????206 | ???156 | ????86 |
| ??B2 | Iso-butylene | ???112 | ???112 | ???156.8 | ????112 | |||
| ??C | ??C1 | Vinyl carbinol | ???14.5 | ????28 | ????28 | ????14.5 | ||
| ??C2 | The alkene ether butyleneglycol vinyl ether of ethylene glycol | ???50 | ???31.5 | ????47 | ????30 | |||
| ??D | The hendecene ester | ???12 | ???18.4 | ????12 | ????15 | ????15 | ????18.4 | |
| Initiator | The Diisopropyl azodicarboxylate benzoyl peroxide | ???6.6 | ???7.0 | ????6.0 | ????6. | ????7.2 | ????6.5 | |
| Solvent | The vinyl acetic monomer N-BUTYL ACETATE | ???200 | ???150 | ????150 | ???150 | ????200 | ????200 | |
| The methylethylketone methyl iso-butyl ketone (MIBK) | ???200 | ???300 | ????200 | ???200 | ????200 ????100 | ????50 ????150 | ||
The characteristic of resulting multipolymer sees Table 2.
Table 2 embodiment 1～6 resulting multipolymer characteristic
| Characteristic | Embodiment | |||||
| ????1 | ????2 | ????3 | ????4 | ????5 | ????6 | |
| Solid content (%) | ????58 | ????56 | ????60 | ????62 | ????55 | ????59 |
| Hydroxyl value (mgkOH/g) | ???82.2 | ???92.0 | ???80.6 | ???84.4 | ???84.6 | ???90.8 |
| Acid number (mgKOH/g) | ????6.0 | ????8.5 | ????6.2 | ????7.8 | ????7.6 | ????8.2 |
| 25 ℃ of seconds of viscosity (being coated with-4 glasss) | ????110 | ????105 | ????120 | ????80 | ????92 | ????88 |
(4) multipolymer that obtains of embodiment 1～6 is made into coating
(1) solid content being diluted to solid content with the N-BUTYL ACETATE equal solvent is 50%, as coating.
(2) add pigment.When being made into whitewash, paint vehicle: titanium dioxide=75: 25.When being made into its allochromatic colour coating, paint vehicle: pigment=90: 10.When adopting carbon black to be made into blackwash, paint vehicle: carbon black=97: 3.(3) grind.Grind with conoidal mill, the fineness that makes coating is below 20 μ m.
Add linking agent when (4) using.Coating is designed to two components, and linking agent adopts HDI (hexamethylene diisocyanate).Consumption is-NCO/-OH=1: 1 (equivalence ratio).
(5) make model by the GB mark, coupon etc. detect its performance.
(5) performance of embodiment 1～6 TFE copolymer coating.
The performance of embodiment 1～6 TFE copolymer coating sees Table 3.
The performance of table 3 embodiment 1～6 TFE copolymer coating
| Project | Performance | Embodiment | ||||||
| ????1 | ????2 | ????3 | ????4 | ????5 | ????6 | |||
| Rerum natura | Sticking power (method of drawing a circle) | ????1 | ????1 | ????2 | ????1 | ????1 | ????1 | |
| Gloss (60 °) (%) | ????68 | ????70 | ????72 | ????75 | ????69 | ????68 | ||
| Hardness (fork method) | ???0.83 | ???0.83 | ???0.85 | ???0.84 | ???0.83 | ???0.85 | ||
| Shock-resistant (cm) | ????50 | ????50 | ????50 | ????50 | ????50 | ????50 | ||
| Flexibility (mm) | ????1 | ????1 | ????2 | ????1 | ????1 | ????1 | ||
| 10%HCl two months | ????○ | ????○ | ????○ | ????○ | ????○ | ????○ | ||
| ??10％H 2SO 4Two months | ????○ | ????○ | ????○ | ????○ | ????○ | ????○ | ||
| 10%NaOH two months | ????○ | ????○ | ????△ | ????△ | ????△ | ????○ | ||
| Dehydrated alcohol one month | ????○ | ????○ | ????○ | ????△ | ????△ | ????○ | ||
| Anti-acetone is cleaned (number of times) | ??＞100 | ??＞100 | ??＞100 | ???＞100 | ??＞100 | ??＞100 | ||
| Anti-artificial promotion is aging | 3000h loss of gloss rate (%) | ????8 | ????5 | ????10 | ????9 | ????11 | ????6 | |
| Salt spray resistance | 3000h (level) | ????1 | ????1 | ????1 | ????2 | ????1 | ????1 | |
Annotate: no change zero changes △ slightly.
Claims (8)
1, a kind of fluoro-containing coating for containing the multiple copolymer of tetrafluoroethylene, is characterized in that the multipolymer based on tetrafluoroethylene, and its chain-like structure synoptic diagram is:
R wherein
1=carbon number is 1～5 normal chain alkyl;
R
2＝(CH
2)n
1，n
1＝0～2；
R
3=carbon number is 1～2 normal chain alkyl;
R
4=carbon number is 1～2 normal chain alkyl;
R
5＝(CH
2)n
2，n
2＝1～4；
R
6＝(CH
2)n
3，n
3＝0～2；
R
7＝(CH
2)n
4，n
4＝2～6；
R
8＝(CH
2)n
5，n
5＝0～8；
A, B, the shared molar percentage of C, D are:
A：50.0～55.0％，
B：35.0～42.0％，
C：6.0～7.5％，
D:0.5～4.0%, wherein B=B
1+ B
2, its mol ratio is B
1: B
2=1.0: 1.0～2.0;
C=C
1+ C
2, its mol ratio is C
1: C
2:=1.0: 1.0～2.5, polymkeric substance is faint yellow transparent thick liquid, and solid content is 52～62%, and hydroxyl value is 80～92mgKOH/g, and acid number is 5.8～8.5mgKOH/g, and proportion is 1.040～1.060, and being coated with-4 glasss of viscosity is 80～120s.
2, fluoro-containing coating as claimed in claim 1 is characterized by in chain-like structure, and the structure of B has only B
1A kind of structure.
3, fluoro-containing coating as claimed in claim 1 is characterized by in chain-like structure, and the structure of C has only C
1Or C
2In a kind of structure.
4, fluoro-containing coating as claimed in claim 1 is characterized by in chain-like structure, when the B structure has only B
1During structure, its C-structure has C
1Or C
2A kind of structure.
5, a kind of manufacture method of the multi-component copolymer body fluoro-containing coating based on tetrafluoroethylene is characterized by and adopts the solution copolymerization method, and used raw material is:
CF
2＝CF
2???????????????????????????????????????????A???
???
CH
2＝CH-R
5-OH??????????????????????????C
1
C
CH
2=CH-R
6-O-R
7-OH C
2 
R wherein
1The normal chain alkyl of=carbon number 1～5;
R
2＝(CH
2)n
1，n
1＝0～2；
R
3The normal chain alkyl of=carbon number 1～2;
R
4The normal chain alkyl of=carbon number 1～2;
R
5＝(CH
2)n
2，n
2＝1～4；
R
6＝(CH
2)n
3，n
3＝0～2；
R
7＝(CH
2)n
4，n
4＝2～6；
R
8=(CH
2) n
5, n
5=0～8; Molar percentage was when four kinds of monomers were participated in reaction:
A：50.0～55.0％
B：35.0～42.0％
C：6.0～7.5％
When D:0.5～4.0% uses monomers B, B=B
1+ B
2, its mol ratio is B
1: B
2=1.0: 1.0～2.0, when using monomer C, C=C
1+ C
2, its mol ratio is:
C
1∶C
2＝1.0∶1.0～2.5；
(2) solvent that uses as the mixture of alkanones and acetates, its weight percent is: alkanones: acetates=60～50%: 40～50%, and described aliphatic ketone is methylethylketone, methyl iso-butyl ketone (MIBK); Described acetic ester is vinyl acetic monomer, N-BUTYL ACETATE; Solvent load is for participating in 30～45% of reaction monomers gross weight;
(3) initiator is azo-compound or acyl peroxide compound, and consumption is 1～3% of a reaction monomers gross weight;
(4) polymerization procedure is: add mixed solvent in the autoclave according to the order of sequence, remove A, B
2Outer monomer, initiator, decompression adds B down
2, A, open to stir, heat up and control reaction temperature is 68～70 ℃, reaction initial pressure is 2.0～2.8MPa, the reaction times is 20～22h, reacts the Bi Jiangwen blowing.
6, the manufacture method of fluoro-containing coating as claimed in claim 5 when it is characterized in that using monomers B, is only used B
1
7, the manufacture method of fluoro-containing coating as claimed in claim 5 is characterized by when using monomer C, only uses C
1Or C
2
8, the manufacture method of fluoro-containing coating as claimed in claim 5 is characterized by and only uses B when using monomers B
1, only use C when using the C monomer simultaneously
1Or C
2
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99113196A CN1111571C (en) | 1999-08-20 | 1999-08-20 | Fluoric copolymer paint and method for making thereof based on tetrafluoroethylene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99113196A CN1111571C (en) | 1999-08-20 | 1999-08-20 | Fluoric copolymer paint and method for making thereof based on tetrafluoroethylene |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1244556A true CN1244556A (en) | 2000-02-16 |
| CN1111571C CN1111571C (en) | 2003-06-18 |
Family
ID=5276412
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99113196A Expired - Fee Related CN1111571C (en) | 1999-08-20 | 1999-08-20 | Fluoric copolymer paint and method for making thereof based on tetrafluoroethylene |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1111571C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1294217C (en) * | 2003-12-15 | 2007-01-10 | 上海三爱富新材料股份有限公司 | Soluble fluorine-containing paint resin and method for preparing same |
| WO2013091381A1 (en) * | 2011-12-22 | 2013-06-27 | 中昊晨光化工研究院有限公司 | Preparation method for polytetrafluoroethylene resin with high fluorine content |
| CN104829772A (en) * | 2015-05-18 | 2015-08-12 | 山东森福新材料有限公司 | Normal temperature cured fluorine-containing coating resin and preparation method thereof |
| US9920214B2 (en) | 2011-03-31 | 2018-03-20 | Daikin Industries, Ltd. | Solvent-based paint composition and fluorine-containing copolymer |
| CN112437795A (en) * | 2018-07-18 | 2021-03-02 | Ａｇｃ株式会社 | Coating material, substrate with coating film, and method for producing substrate with coating film |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0637604B2 (en) * | 1988-05-17 | 1994-05-18 | セントラル硝子株式会社 | Fluorine-containing copolymer for paint |
| FR2636336B1 (en) * | 1988-09-13 | 1993-12-24 | Central Glass Cy Ltd | COPOLYMER CONTAINING FLUORINE USEFUL AS PAINT VEHICLE |
-
1999
- 1999-08-20 CN CN99113196A patent/CN1111571C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1294217C (en) * | 2003-12-15 | 2007-01-10 | 上海三爱富新材料股份有限公司 | Soluble fluorine-containing paint resin and method for preparing same |
| US9920214B2 (en) | 2011-03-31 | 2018-03-20 | Daikin Industries, Ltd. | Solvent-based paint composition and fluorine-containing copolymer |
| WO2013091381A1 (en) * | 2011-12-22 | 2013-06-27 | 中昊晨光化工研究院有限公司 | Preparation method for polytetrafluoroethylene resin with high fluorine content |
| CN104829772A (en) * | 2015-05-18 | 2015-08-12 | 山东森福新材料有限公司 | Normal temperature cured fluorine-containing coating resin and preparation method thereof |
| CN112437795A (en) * | 2018-07-18 | 2021-03-02 | Ａｇｃ株式会社 | Coating material, substrate with coating film, and method for producing substrate with coating film |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1111571C (en) | 2003-06-18 |
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