CN118812898A - A preparation method and application of polytetrafluoroethylene ceramic composite membrane - Google Patents
A preparation method and application of polytetrafluoroethylene ceramic composite membrane Download PDFInfo
- Publication number
- CN118812898A CN118812898A CN202411297917.2A CN202411297917A CN118812898A CN 118812898 A CN118812898 A CN 118812898A CN 202411297917 A CN202411297917 A CN 202411297917A CN 118812898 A CN118812898 A CN 118812898A
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- CN
- China
- Prior art keywords
- polytetrafluoroethylene
- ceramic composite
- composite membrane
- weight
- parts
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 229920001343 polytetrafluoroethylene Polymers 0.000 title claims abstract description 204
- 239000004810 polytetrafluoroethylene Substances 0.000 title claims abstract description 204
- -1 polytetrafluoroethylene Polymers 0.000 title claims abstract description 187
- 239000000919 ceramic Substances 0.000 title claims abstract description 134
- 239000002131 composite material Substances 0.000 title claims abstract description 79
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- 239000012528 membrane Substances 0.000 title claims description 96
- 238000000034 method Methods 0.000 claims abstract description 65
- 239000000945 filler Substances 0.000 claims abstract description 64
- 239000000463 material Substances 0.000 claims abstract description 47
- 239000000839 emulsion Substances 0.000 claims abstract description 45
- 239000002904 solvent Substances 0.000 claims abstract description 40
- 238000000576 coating method Methods 0.000 claims abstract description 29
- 239000000843 powder Substances 0.000 claims description 104
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 83
- 239000000377 silicon dioxide Substances 0.000 claims description 40
- 229910052582 BN Inorganic materials 0.000 claims description 38
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 claims description 36
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 35
- 238000007731 hot pressing Methods 0.000 claims description 35
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 28
- 239000011248 coating agent Substances 0.000 claims description 21
- 239000006254 rheological additive Substances 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 20
- 239000003365 glass fiber Substances 0.000 claims description 16
- 238000004821 distillation Methods 0.000 claims description 15
- 239000011256 inorganic filler Substances 0.000 claims description 14
- 229910003475 inorganic filler Inorganic materials 0.000 claims description 14
- 238000003475 lamination Methods 0.000 claims description 14
- 238000005245 sintering Methods 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 12
- 239000011889 copper foil Substances 0.000 claims description 11
- 239000011888 foil Substances 0.000 claims description 11
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 10
- 229920001721 polyimide Polymers 0.000 claims description 10
- KPDTTZWHFZUVCL-UHFFFAOYSA-N 1-prop-2-enylimidazolidine-2,4-dione Chemical compound C=CCN1CC(=O)NC1=O KPDTTZWHFZUVCL-UHFFFAOYSA-N 0.000 claims description 8
- 235000012239 silicon dioxide Nutrition 0.000 claims description 8
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 7
- 229910052782 aluminium Inorganic materials 0.000 claims description 7
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 6
- 239000012046 mixed solvent Substances 0.000 claims description 5
- 239000004408 titanium dioxide Substances 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims description 4
- 239000000835 fiber Substances 0.000 claims description 4
- 239000011521 glass Substances 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 238000005520 cutting process Methods 0.000 claims description 3
- 238000010030 laminating Methods 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 2
- 229910052454 barium strontium titanate Inorganic materials 0.000 claims description 2
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 claims description 2
- 229910002113 barium titanate Inorganic materials 0.000 claims description 2
- 239000011324 bead Substances 0.000 claims description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- 229920001577 copolymer Polymers 0.000 claims description 2
- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 claims description 2
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 2
- 239000000347 magnesium hydroxide Substances 0.000 claims description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 2
- 239000010445 mica Substances 0.000 claims description 2
- 229910052618 mica group Inorganic materials 0.000 claims description 2
- 239000010453 quartz Substances 0.000 claims description 2
- 239000011787 zinc oxide Substances 0.000 claims description 2
- 238000005098 hot rolling Methods 0.000 claims 2
- 239000011159 matrix material Substances 0.000 claims 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims 1
- 238000003490 calendering Methods 0.000 abstract description 33
- 230000007547 defect Effects 0.000 abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 238000004891 communication Methods 0.000 abstract description 5
- 239000002648 laminated material Substances 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 55
- 229920005989 resin Polymers 0.000 description 37
- 239000011347 resin Substances 0.000 description 37
- 239000003849 aromatic solvent Substances 0.000 description 34
- 229910052802 copper Inorganic materials 0.000 description 24
- 239000010949 copper Substances 0.000 description 24
- 239000003292 glue Substances 0.000 description 24
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 16
- 238000009835 boiling Methods 0.000 description 16
- 239000002245 particle Substances 0.000 description 16
- 239000008096 xylene Substances 0.000 description 16
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 239000011231 conductive filler Substances 0.000 description 10
- 239000000243 solution Substances 0.000 description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 8
- 239000011259 mixed solution Substances 0.000 description 8
- 239000002002 slurry Substances 0.000 description 8
- 238000011056 performance test Methods 0.000 description 7
- 239000000758 substrate Substances 0.000 description 7
- 238000012360 testing method Methods 0.000 description 6
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 6
- 239000002562 thickening agent Substances 0.000 description 6
- 239000004744 fabric Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 229940010514 ammonium ferrous sulfate Drugs 0.000 description 4
- 239000012153 distilled water Substances 0.000 description 4
- IMBKASBLAKCLEM-UHFFFAOYSA-L ferrous ammonium sulfate (anhydrous) Chemical compound [NH4+].[NH4+].[Fe+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O IMBKASBLAKCLEM-UHFFFAOYSA-L 0.000 description 4
- 238000002329 infrared spectrum Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000004804 winding Methods 0.000 description 4
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 3
- 239000004642 Polyimide Substances 0.000 description 3
- 239000006087 Silane Coupling Agent Substances 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 229910052731 fluorine Inorganic materials 0.000 description 3
- 239000011737 fluorine Substances 0.000 description 3
- 238000007655 standard test method Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 229920000295 expanded polytetrafluoroethylene Polymers 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 238000009775 high-speed stirring Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 230000002787 reinforcement Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 238000012795 verification Methods 0.000 description 2
- 229920001410 Microfiber Polymers 0.000 description 1
- 238000000944 Soxhlet extraction Methods 0.000 description 1
- 239000002313 adhesive film Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000011162 core material Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012765 fibrous filler Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000003658 microfiber Substances 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 102220043159 rs587780996 Human genes 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29D—PRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
- B29D7/00—Producing flat articles, e.g. films or sheets
- B29D7/01—Films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B15/00—Layered products comprising a layer of metal
- B32B15/04—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B15/08—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
- B32B15/085—Layered products comprising a layer of metal comprising metal as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B15/00—Layered products comprising a layer of metal
- B32B15/20—Layered products comprising a layer of metal comprising aluminium or copper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
- B32B27/322—Layered products comprising a layer of synthetic resin comprising polyolefins comprising halogenated polyolefins, e.g. PTFE
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K1/00—Printed circuits
- H05K1/02—Details
- H05K1/03—Use of materials for the substrate
- H05K1/0313—Organic insulating material
- H05K1/0353—Organic insulating material consisting of two or more materials, e.g. two or more polymers, polymer + filler, + reinforcement
- H05K1/036—Multilayers with layers of different types
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/20—Properties of the layers or laminate having particular electrical or magnetic properties, e.g. piezoelectric
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2307/00—Properties of the layers or laminate
- B32B2307/30—Properties of the layers or laminate having particular thermal properties
- B32B2307/302—Conductive
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2427/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2427/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2427/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2427/18—Homopolymers or copolymers of tetrafluoroethylene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
- C08K2003/2237—Oxides; Hydroxides of metals of titanium
- C08K2003/2241—Titanium dioxide
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/02—Fibres or whiskers
- C08K7/04—Fibres or whiskers inorganic
- C08K7/14—Glass
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/16—Solid spheres
- C08K7/18—Solid spheres inorganic
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
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- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
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Abstract
本发明公开了一种聚四氟乙烯陶瓷复合膜的制备方法及其应用,涉及通讯材料制造领域。本发明通过涂布工艺,溶剂的分步挥发,分步连续热压延,即采用涂覆法制备聚四氟乙烯陶瓷生膜,使生膜经过分步“热处理‑热压延”处理,实现了聚四氟乙烯陶瓷膜的连续成卷生产;另外,本发明采用连续热压延的方法,逐渐提高材料密度,消除成膜缺陷,制备的复合膜密度均匀,厚度均一,拉伸断裂强度优于现有水性乳液涂覆工艺生产的复合膜;且本发明所述方法可以获得具有高导热性能、高填料量的聚四氟乙烯陶瓷复合膜以及高导热的高频覆铜板材料;且具备高导热性和高频下的低介电损耗特性,适用于对热管理有较高要求的大功率高频高速印制线路板产品。
The present invention discloses a preparation method and application of a polytetrafluoroethylene ceramic composite film, and relates to the field of communication material manufacturing. The present invention adopts a coating process, a step-by-step volatilization of a solvent, and a step-by-step continuous hot calendering, that is, a coating method is used to prepare a polytetrafluoroethylene ceramic raw film, so that the raw film is subjected to a step-by-step "heat treatment-hot calendering" treatment, thereby realizing the continuous roll production of the polytetrafluoroethylene ceramic film; in addition, the present invention adopts a continuous hot calendering method to gradually increase the material density and eliminate film-forming defects, and the prepared composite film has uniform density and thickness, and the tensile fracture strength is better than the composite film produced by the existing aqueous emulsion coating process; and the method described in the present invention can obtain a polytetrafluoroethylene ceramic composite film with high thermal conductivity and high filler content, as well as a high-frequency copper-clad laminate material with high thermal conductivity; and it has high thermal conductivity and low dielectric loss characteristics at high frequencies, and is suitable for high-power, high-frequency, and high-speed printed circuit board products with high requirements for thermal management.
Description
技术领域Technical Field
本发明属于通讯材料制造领域,特别涉及一种聚四氟乙烯陶瓷复合膜的制备方法及其应用。The invention belongs to the field of communication material manufacturing, and particularly relates to a preparation method of a polytetrafluoroethylene ceramic composite film and application thereof.
背景技术Background Art
目前,在4G、5G乃至于毫米波通讯的实际应用中,尤其是5G或毫米波通讯应用的高频印制电路板基材(高频PCB基材)领域,对于材料本身的介电常数与介电损耗、以及材料的导热性能有着越来越高的要求。其中,PTFE材料以其独特的介电常数稳定性与所有高分子材料中极低的介电损耗性能,在上述应用中发挥着无可替代的作用,是几种核心材料之一。膨体聚四氟乙烯膜一般以双向拉伸工艺制成,由于其中含有空隙,因此无法用作5G或毫米波通讯的基板材料;而非膨体工艺制备的聚四氟乙烯陶瓷复合膜材料越来越受到本领域国内外研究人员的广泛关注,有着巨大的工业应用市场和前景。At present, in the practical applications of 4G, 5G and even millimeter wave communications, especially in the field of high-frequency printed circuit board substrates (high-frequency PCB substrates) for 5G or millimeter wave communications, there are increasingly higher requirements for the dielectric constant and dielectric loss of the material itself, as well as the thermal conductivity of the material. Among them, PTFE material plays an irreplaceable role in the above applications with its unique dielectric constant stability and extremely low dielectric loss performance among all polymer materials, and is one of several core materials. Expanded polytetrafluoroethylene film is generally made by a biaxial stretching process. Because it contains voids, it cannot be used as a substrate material for 5G or millimeter wave communications; while polytetrafluoroethylene ceramic composite membrane materials prepared by non-expanded process are increasingly attracting widespread attention from researchers at home and abroad in this field, and have a huge industrial application market and prospects.
目前,聚四氟乙烯陶瓷复合膜材料的制备主要有以下几种路线:At present, there are mainly the following routes for the preparation of polytetrafluoroethylene ceramic composite membrane materials:
(1)、玻纤浸涂法(1) Glass fiber dipping method
以PTFE-编织玻璃纤维布浸涂工艺制备的PTFE-玻纤布,其工艺简单,技术难度较低,但是其中所含的编织玻璃纤维布带来的网孔效应,限制了材料在毫米波领域的应用,并且为非各项同性材料;The PTFE-glass fiber cloth prepared by the PTFE-woven glass fiber cloth dip coating process has a simple process and low technical difficulty, but the mesh effect brought by the woven glass fiber cloth contained therein limits the application of the material in the millimeter wave field, and it is a non-isotropic material;
(2)、模压车削法(2) Die turning method
采用了“混合-模压-烧结-车削”的工艺路线,制备一种不含玻纤布增强的聚四氟乙烯陶瓷复合膜材料;车削工艺可以连续生产,成本较低,膜厚度15-50μm,可调节;但是车削工艺限制了材料中的陶瓷含量,其中的陶瓷含量普遍不大于10wt%,制备更高填料含量的车削膜表面缺陷多;The process of "mixing-molding-sintering-turning" was adopted to prepare a polytetrafluoroethylene ceramic composite membrane material without glass fiber cloth reinforcement; the turning process can be produced continuously, with low cost, and the membrane thickness is 15-50μm, which can be adjusted; however, the turning process limits the ceramic content in the material, and the ceramic content is generally not more than 10wt%, and the turning membrane with higher filler content has many surface defects;
(3)、挤出压延法(3) Extrusion calendering method
US4335180A公开了向PTFE乳液中先后混入微纤维、无机填料和絮凝剂,后经过滤-干燥等步骤得到含氟树脂混合物,压制成板后,与铜箔叠合在一起再压合得到无玻纤布增强的含氟树脂基覆铜板;此方法片材厚度较大,无法实现连续化生产制备聚四氟乙烯膜,且生产过程中还会产生大量含氟化合物废水;US4335180A discloses that microfibers, inorganic fillers and flocculants are mixed into PTFE emulsion in sequence, and then filtered and dried to obtain a fluorine-containing resin mixture, which is pressed into a plate and then laminated with copper foil to obtain a fluorine-containing resin-based copper-clad laminate without glass fiber cloth reinforcement. This method has a large sheet thickness and cannot achieve continuous production of polytetrafluoroethylene membranes. In addition, a large amount of fluorine-containing compound wastewater is generated during the production process.
中国专利CN2013100250727介绍了一种高填料含量的PTFE覆铜板的制备方法:首先将氟树脂粉末与无机填料进行混合,然后加入有机润滑剂,搅拌成面团状物体,再进行挤出、压延等工序,得到片材,对该片材进行热(250℃/6h)处理,再用氟树脂分散乳液浸渍该片材,并进行干燥、烘培、烧结,得到孔隙少、表面覆了一层树脂膜的片材;此方法同样无法实现连续化生产制备聚四氟乙烯膜;Chinese patent CN2013100250727 introduces a method for preparing a PTFE copper-clad laminate with a high filler content: first, fluororesin powder is mixed with an inorganic filler, then an organic lubricant is added, and the mixture is stirred into a dough-like object, and then extrusion, calendering and other processes are performed to obtain a sheet, the sheet is heat-treated (250°C/6h), and then the sheet is impregnated with a fluororesin dispersion, and then dried, baked and sintered to obtain a sheet with few pores and a layer of resin film on the surface; this method also cannot achieve continuous production of polytetrafluoroethylene membranes;
(4)、水性乳液涂覆-烧结工艺(4) Water-based emulsion coating-sintering process
中国专利CN104175686A公开了将氟树脂乳液、无机填料和增稠剂混合后制得分散液,然后将分散液涂覆在可离型的基材上烘烤,后将树脂层与基材分离,再经裁剪、叠合和烧结等工艺制备复合介质基板;Chinese patent CN104175686A discloses that a fluororesin emulsion, an inorganic filler and a thickener are mixed to obtain a dispersion, and then the dispersion is coated on a releasable substrate and baked, and then the resin layer is separated from the substrate, and then a composite dielectric substrate is prepared by cutting, laminating and sintering.
天津四十六所相关课题组将PTFE水性乳液、陶瓷粉填料、表面活性剂、硅烷偶联剂、增稠剂等原料配制成浆液,采用涂覆-烧结的方式,在聚酰亚胺底膜-镜面不锈钢钢带上实现聚四氟乙烯陶瓷膜的生产工艺;The relevant research group of Tianjin No. 46 Institute prepared PTFE water-based emulsion, ceramic powder filler, surfactant, silane coupling agent, thickener and other raw materials into slurry, and realized the production process of polytetrafluoroethylene ceramic membrane on polyimide base film-mirror stainless steel belt by coating-sintering method;
但是,按照上述路线公开的工艺,所制作出的薄膜微观缺陷产生较多(裂纹,孔隙等),材料的致密性有待改善;此外,该路线通过增稠剂的方式,所添加的陶瓷填料含量依然有限;而过高的添加量会导致上述工艺无法获得持续稳定的浆料。However, according to the process disclosed in the above route, the film produced has many microscopic defects (cracks, pores, etc.), and the density of the material needs to be improved; in addition, the content of ceramic fillers added by thickeners in this route is still limited; and too high an addition amount will cause the above process to be unable to obtain a continuously stable slurry.
可见,聚四氟乙烯自身属于热塑性树脂材料,但是PTFE本身的熔体粘度极高,在熔融温度之上也几乎不流动,很难通过普通热塑性树脂的方法加工成型。因此考虑到已有路线的不足之处和PTFE材料自身的特点,开发新的聚四氟乙烯陶瓷复合膜的成型工艺有着重大的技术和应用意义。It can be seen that polytetrafluoroethylene itself is a thermoplastic resin material, but the melt viscosity of PTFE itself is extremely high, and it almost does not flow above the melting temperature, making it difficult to process and shape using ordinary thermoplastic resin methods. Therefore, considering the shortcomings of existing routes and the characteristics of PTFE materials themselves, the development of a new molding process for polytetrafluoroethylene ceramic composite membranes has great technical and application significance.
发明内容Summary of the invention
本发明的主要目的是:一方面提供一种可量产的且品质稳定的聚四氟乙烯陶瓷复合膜的制备方法,以减少现有水性乳液涂覆-烧结工艺的生产过程中出现膜的厚度及性能不均一、不稳定,以及表观存在缺陷的问题;另一方面提供一种高导热聚四氟乙烯陶瓷复合膜的制备方法及其应用,用于制备导热率不小于1.2W/(m•K)的高导热聚四氟乙烯陶瓷基高频覆铜板。The main objectives of the present invention are: on the one hand, to provide a method for preparing a polytetrafluoroethylene ceramic composite membrane that can be mass-produced and has stable quality, so as to reduce the problems of uneven thickness and performance, instability, and surface defects in the production process of the existing aqueous emulsion coating-sintering process; on the other hand, to provide a method for preparing a high thermal conductivity polytetrafluoroethylene ceramic composite membrane and its application, which are used to prepare a high thermal conductivity polytetrafluoroethylene ceramic-based high-frequency copper clad laminate with a thermal conductivity of not less than 1.2W/(m•K).
作为本发明的第一方面,为达到上述目的,本发明提供的聚四氟乙烯陶瓷复合膜的制备方法,包含如下步骤:As a first aspect of the present invention, in order to achieve the above-mentioned purpose, the present invention provides a method for preparing a polytetrafluoroethylene ceramic composite membrane, comprising the following steps:
步骤1、将氟树脂粉末、无机填料粉末、流变助剂和芳香烃混合溶剂充分混合,得到溶剂型乳液;Step 1, fully mixing fluororesin powder, inorganic filler powder, rheological additive and aromatic hydrocarbon mixed solvent to obtain a solvent-based emulsion;
步骤2、将步骤1中的溶剂型乳液涂覆于基膜上,在70-150℃下进行第一次烘烤处理,制备出涂覆在膜上的聚四氟乙烯陶瓷生膜卷材;Step 2, coating the solvent-based emulsion in step 1 on the base film, and performing a first baking treatment at 70-150° C. to prepare a polytetrafluoroethylene ceramic raw film coil coated on the film;
步骤3、进行第一次连续热压延处理,热压温度80-140℃;Step 3, performing the first continuous hot calendering treatment, the hot pressing temperature is 80-140°C;
步骤4、在200-280℃下进行第二次烘烤;Step 4, baking for the second time at 200-280°C;
步骤5、进行第二次连续热压延处理,热压温度80-140℃,获得复合基膜的聚四氟乙烯陶瓷膜卷材;Step 5, performing a second continuous hot calendering treatment at a hot pressing temperature of 80-140° C. to obtain a polytetrafluoroethylene ceramic membrane coil of a composite base membrane;
步骤6、进行330-380℃高温烧结,冷却后制得聚四氟乙烯陶瓷复合膜。Step 6: sintering at a high temperature of 330-380° C. and obtaining a polytetrafluoroethylene ceramic composite membrane after cooling.
具体地,上述聚四氟乙烯陶瓷复合膜的生产工艺,包括如下步骤:Specifically, the production process of the above-mentioned polytetrafluoroethylene ceramic composite membrane includes the following steps:
步骤1、将氟树脂粉末、无机填料粉末、流变助剂、和高/低沸点芳香烃溶剂充分混合,得到分散均匀的溶剂型乳液;Step 1, fully mixing fluororesin powder, inorganic filler powder, rheological additive, and high/low boiling point aromatic hydrocarbon solvent to obtain a uniformly dispersed solvent-based emulsion;
步骤2、采用卧式涂覆设备,将步骤1中所述乳液定量、均匀地涂覆于膜上;经过分段温度烘烤处理,各分段温度设置范围均为70-150℃,总停留时间为3-10min(各温度段停留时间相同),挥发掉体系中的低沸点芳香烃溶剂,制备出涂覆在膜上的聚四氟乙烯陶瓷生膜卷材;Step 2: using a horizontal coating device, quantitatively and evenly coating the emulsion in step 1 on the membrane; after a segmented temperature baking treatment, the temperature setting range of each segment is 70-150° C., and the total residence time is 3-10 min (the residence time of each temperature segment is the same), the low boiling point aromatic hydrocarbon solvent in the system is volatilized, and a polytetrafluoroethylene ceramic raw membrane coil coated on the membrane is prepared;
步骤3、将步骤2制备的生膜进行第一次连续热压延处理,热压温度80-140℃,热压延线速度为0.2-3m/min,压延辊顶压5-60t,消除膜材料中的微孔,获得复合基膜的、含有高沸点芳香烃溶剂的聚四氟乙烯陶瓷膜卷材;Step 3, subjecting the raw membrane prepared in step 2 to a first continuous hot calendering treatment, with a hot pressing temperature of 80-140° C., a hot calendering line speed of 0.2-3 m/min, and a calendering roller top pressure of 5-60 t, to eliminate micropores in the membrane material, and obtain a composite base membrane containing a polytetrafluoroethylene ceramic membrane coil containing a high-boiling point aromatic hydrocarbon solvent;
步骤4、将步骤3制备的卷材通过隧道式通风烘箱,烘箱温度分段设置,各分段温度设置范围均为200-280℃,总停留时间为2-10min(各温度段停留时间相同),挥发其中的高沸点芳香烃溶剂;Step 4, passing the coil prepared in step 3 through a tunnel ventilation oven, wherein the oven temperature is set in sections, each section temperature setting range is 200-280°C, and the total residence time is 2-10min (the residence time in each temperature section is the same), to volatilize the high boiling point aromatic hydrocarbon solvent therein;
步骤5、将步骤4处理后的卷材在连续热压延机上,进行第二次连续热压延处理,热压温度80-140℃,热压延线速度为0.2-3m/min,压延辊顶压5-60t,获得复合基膜的聚四氟乙烯陶瓷膜卷材;Step 5, subjecting the coiled material treated in step 4 to a second continuous hot calendering treatment on a continuous hot calendering machine, with a hot pressing temperature of 80-140° C., a hot calendering line speed of 0.2-3 m/min, and a calendering roller top pressure of 5-60 t, to obtain a polytetrafluoroethylene ceramic membrane coiled material of a composite base membrane;
步骤6、将步骤5处理后的卷材在高温烘箱中烧结,烧结温度330-380℃,烧结时间1-8h。冷却后,制得聚四氟乙烯陶瓷复合膜。Step 6: sinter the coiled material treated in step 5 in a high temperature oven at a sintering temperature of 330-380° C. for 1-8 hours. After cooling, a polytetrafluoroethylene ceramic composite membrane is obtained.
优选地,所述氟树脂粉末,包含第一组分和第二组分;所述第一组分选自聚四氟乙烯(PTFE)或改性聚四氟乙烯中的至少一种;所述第二组分选自四氟乙烯-全氟烷基乙烯基醚共聚物(PFA)或聚全氟乙丙烯(FEP)中的任意一种或两种。Preferably, the fluororesin powder comprises a first component and a second component; the first component is selected from at least one of polytetrafluoroethylene (PTFE) or modified polytetrafluoroethylene; the second component is selected from any one or both of tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (PFA) or polyperfluoroethylene propylene (FEP).
优选地,以所有氟树脂粉末重量为100份,第一组分的重量不低于85份。Preferably, the weight of the first component is not less than 85 parts based on 100 parts by weight of the entire fluororesin powder.
优选地,所述氟树脂粉末为悬浮细粉,粒径为20-40μm。Preferably, the fluororesin powder is a suspended fine powder with a particle size of 20-40 μm.
优选地,所述无机填料粉末为包含二氧化硅、玻璃粉、空心玻璃珠、二氧化钛、钛酸钡、钛酸锶钡、氧化铝、氮化铝、氮化硼、碳酸钙、氢氧化铝、氢氧化镁、云母、玻璃纤维、石英纤维、氧化锌中的一种或几种的混合物。Preferably, the inorganic filler powder is a mixture of one or more of silicon dioxide, glass powder, hollow glass beads, titanium dioxide, barium titanate, barium strontium titanate, aluminum oxide, aluminum nitride, boron nitride, calcium carbonate, aluminum hydroxide, magnesium hydroxide, mica, glass fiber, quartz fiber, and zinc oxide.
优选地,所述无机填料粉末的用量占氟树脂和填料总体积的5vol%至75vol%。Preferably, the amount of the inorganic filler powder used accounts for 5 vol% to 75 vol% of the total volume of the fluororesin and the filler.
优选地,所述流变助剂,为溶剂型流变助剂,用于提高乳液的防沉降性能。Preferably, the rheological additive is a solvent-based rheological additive, which is used to improve the anti-settling performance of the emulsion.
优选地,所述流变助剂的用量为氟树脂重量的0.05-0.5wt%。Preferably, the rheological additive is used in an amount of 0.05-0.5 wt % of the weight of the fluororesin.
优选地,所述芳香烃混合溶剂,包含由一种或几种馏程为100-200℃的芳香烃溶剂,和一种或几种馏程为230-350℃的芳香烃溶剂,组成的混合溶剂或润滑助剂。Preferably, the aromatic hydrocarbon mixed solvent comprises a mixed solvent or lubricating aid composed of one or more aromatic hydrocarbon solvents with a distillation range of 100-200°C and one or more aromatic hydrocarbon solvents with a distillation range of 230-350°C.
优选地,以全部氟树脂为100重量份,所述一种或几种馏程为100-200℃的芳香烃溶剂的加入量为20-70重量份;所述一种或几种馏程为230-350℃的芳香烃溶剂的加入量为5-15重量份。Preferably, based on 100 parts by weight of the total fluororesin, the amount of the one or more aromatic hydrocarbon solvents with a distillation range of 100-200° C. added is 20-70 parts by weight; the amount of the one or more aromatic hydrocarbon solvents with a distillation range of 230-350° C. added is 5-15 parts by weight.
优选地,所述一种或几种馏程为100-200℃的芳香烃溶剂,举例为,混合二甲苯(馏程 137-143℃)、和馏程 161-179℃的芳香烃溶剂的其中一种或两种的混合物。Preferably, the one or more aromatic hydrocarbon solvents with a distillation range of 100-200°C are, for example, mixed xylene (distillation range 137-143°C) and a mixture of one or two of aromatic hydrocarbon solvents with a distillation range of 161-179°C.
优选地,所述一种或几种馏程为230-350℃的芳香烃溶剂,举例为馏程246-304 ℃的芳香烃溶剂、馏程215-295 ℃的芳香烃溶剂、馏程300-350 ℃的芳香烃溶剂中的一种或两种混合物。Preferably, the one or more aromatic hydrocarbon solvents with a distillation range of 230-350°C are, for example, one or a mixture of two of an aromatic hydrocarbon solvent with a distillation range of 246-304°C, an aromatic hydrocarbon solvent with a distillation range of 215-295°C, and an aromatic hydrocarbon solvent with a distillation range of 300-350°C.
优选地,所述基膜为聚酰亚胺膜、铝箔、铜箔、不锈钢箔中的任意一种。Preferably, the base film is any one of polyimide film, aluminum foil, copper foil and stainless steel foil.
优选地,所述步骤2、步骤4中挥发的芳香烃溶剂,可回收后再次使用。Preferably, the aromatic hydrocarbon solvent volatilized in step 2 and step 4 can be recovered and reused.
作为本发明的第二方面,还提供一种高导热聚四氟乙烯陶瓷复合膜的制备方法,与上述聚四氟乙烯陶瓷复合膜的制备方法不同的是,高导热聚四氟乙烯陶瓷复合膜的制备方法所提供的组分中无机填料粉末需满足如下要求:所述无机填料粉末为球形二氧化硅、球形氧化铝、片状氮化硼和球形氮化硼的混合填料。As a second aspect of the present invention, a method for preparing a high thermal conductivity polytetrafluoroethylene ceramic composite membrane is also provided. Different from the above-mentioned method for preparing a polytetrafluoroethylene ceramic composite membrane, the inorganic filler powder in the components provided by the method for preparing a high thermal conductivity polytetrafluoroethylene ceramic composite membrane must meet the following requirements: the inorganic filler powder is a mixed filler of spherical silica, spherical alumina, flaky boron nitride and spherical boron nitride.
优选地,所述混合填料的用量占氟树脂和填料总体积的50vol%至75vol%。Preferably, the amount of the mixed filler is 50 vol% to 75 vol% of the total volume of the fluororesin and the filler.
优选地,所述混合填料的用量占氟树脂和填料总体积的55vol%至65vol%。Preferably, the amount of the mixed filler is 55 vol% to 65 vol% of the total volume of the fluororesin and the filler.
优选地,所述球形二氧化硅、球形氧化铝的粒径为1-5μm。Preferably, the particle size of the spherical silica and spherical alumina is 1-5 μm.
优选地,所述片状氮化硼的片状颗粒粒径为10-20μm。Preferably, the flake particles of the flake boron nitride have a particle size of 10-20 μm.
优选地,所述球形氮化硼的颗粒粒径为:50-100μm。Preferably, the particle size of the spherical boron nitride is 50-100 μm.
优选地,所述无机填料粉末为采用硅烷偶联剂表面处理过的填料粉末。Preferably, the inorganic filler powder is a filler powder surface-treated with a silane coupling agent.
优选地,以所述混合填料总体积为100份,球形氮化硼体积比为10-20vol%,片状氮化硼体积比为15-30vol%,球形二氧化硅和球形氧化铝总量的体积比为50-75vol%;所述混合填料中球形二氧化硅与球形氧化铝以任意比例混合。Preferably, with the total volume of the mixed filler being 100 parts, the volume ratio of spherical boron nitride is 10-20 vol%, the volume ratio of flaky boron nitride is 15-30 vol%, and the volume ratio of the total amount of spherical silica and spherical alumina is 50-75 vol%; spherical silica and spherical alumina in the mixed filler are mixed in any proportion.
作为本发明的第二方面,还提供一种高导热聚四氟乙烯陶瓷复合膜的应用,用于制备高导热高频覆铜板,将按照上述制备方法所制备的高导热聚四氟乙烯陶瓷复合膜裁切后,将其一层或多层叠合后,两侧或单侧覆上铜箔,在真空高温压机中进行层压,得到所述高导热高频覆铜板。As a second aspect of the present invention, an application of a high thermal conductivity polytetrafluoroethylene ceramic composite film is also provided for preparing a high thermal conductivity high frequency copper clad laminate. The high thermal conductivity polytetrafluoroethylene ceramic composite film prepared according to the above preparation method is cut, one or more layers are stacked, copper foil is coated on both sides or one side, and laminated in a vacuum high temperature press to obtain the high thermal conductivity high frequency copper clad laminate.
优选地,厚度为1.0mm的高导热高频覆铜板的导热率不小于1.2W/(m•K)。Preferably, the thermal conductivity of the high thermal conductivity high frequency copper clad laminate with a thickness of 1.0 mm is not less than 1.2 W/(m•K).
优选地,所述高温层压的温度为350-400℃。Preferably, the temperature of the high temperature lamination is 350-400°C.
本发明中的“高导热”是指,按照ASTMD5470方法规定,采用标准热流法,测试介质厚度为1.0mm硬质覆铜板基材的导热率不小于1.2W/(m•K)。The "high thermal conductivity" in the present invention means that according to the ASTM D5470 method, using the standard heat flow method, the thermal conductivity of the hard copper clad laminate substrate with a test medium thickness of 1.0 mm is not less than 1.2 W/(m•K).
本发明还公开了一种改性聚四氟乙烯的制备方法,包括:采用1-烯丙基乙内酰脲与聚四氟乙烯发生接枝反应,获得改性聚四氟乙烯。The invention also discloses a method for preparing modified polytetrafluoroethylene, comprising: using 1-allylhydantoin to carry out a grafting reaction with polytetrafluoroethylene to obtain the modified polytetrafluoroethylene.
本发明采用1-烯丙基乙内酰脲为改性剂,接枝改性聚四氟乙烯,然后再将改性聚四氟乙烯用于聚四氟乙烯陶瓷膜的制备,使获得的聚四氟乙烯陶瓷膜具有良好的密度及拉伸强度。The invention adopts 1-allylhydantoin as a modifier to graft-modify polytetrafluoroethylene, and then uses the modified polytetrafluoroethylene for preparing a polytetrafluoroethylene ceramic membrane, so that the obtained polytetrafluoroethylene ceramic membrane has good density and tensile strength.
具体地,上述改性聚四氟乙烯的制备方法,包括以下步骤:Specifically, the preparation method of the modified polytetrafluoroethylene comprises the following steps:
将聚四氟乙烯在60Co放射源中进行γ射线辐照45-55kGy,然后将辐照后的聚四氟乙烯加入到乙醇和蒸馏水的混合液中,再加入1-烯丙基乙内酰脲、硫酸亚铁铵和浓度为90-95wt%的浓硫酸,氮气氛围下,升温至60-70℃,反应4-7h,过滤,索氏抽提55-65h,干燥,获得改性聚四氟乙烯。The polytetrafluoroethylene is irradiated with 45-55 kGy of gamma rays in a 60 Co radiation source, and then the irradiated polytetrafluoroethylene is added to a mixture of ethanol and distilled water, and then 1-allylhydantoin, ammonium ferrous sulfate and concentrated sulfuric acid with a concentration of 90-95 wt% are added. Under a nitrogen atmosphere, the temperature is raised to 60-70° C., the reaction is carried out for 4-7 hours, the mixture is filtered, Soxhlet extraction is carried out for 55-65 hours, and the mixture is dried to obtain modified polytetrafluoroethylene.
优选地,上述聚四氟乙烯与混合液的质量体积比为1g:15-20mL;乙醇与蒸馏水的体积比为1:2-3;1-烯丙基乙内酰脲在混合液中的浓度为20-30wt%;硫酸亚铁铵在混合液中的浓度为0.08-0.15g/L;浓硫酸在混合液中的浓度为0.7-1.3mL/L。Preferably, the mass volume ratio of the above-mentioned polytetrafluoroethylene to the mixed solution is 1g:15-20mL; the volume ratio of ethanol to distilled water is 1:2-3; the concentration of 1-allylhydantoin in the mixed solution is 20-30wt%; the concentration of ammonium ferrous sulfate in the mixed solution is 0.08-0.15g/L; and the concentration of concentrated sulfuric acid in the mixed solution is 0.7-1.3mL/L.
本发明的有益效果:Beneficial effects of the present invention:
1、与现有溶剂型聚四氟乙烯陶瓷基高频板所采用的挤出压延生产工艺相比,本发明通过涂布工艺,溶剂的分步挥发,分步连续热压延,即采用涂覆法制备聚四氟乙烯陶瓷生膜,使生膜经过分步“热处理-热压延”处理,实现了聚四氟乙烯陶瓷膜的连续成卷生产;1. Compared with the extrusion and calendering production process used in the existing solvent-based polytetrafluoroethylene ceramic-based high-frequency board, the present invention adopts a coating process, a step-by-step volatilization of the solvent, and a step-by-step continuous hot calendering, that is, a coating method is used to prepare the polytetrafluoroethylene ceramic green film, and the green film is subjected to a step-by-step "heat treatment-hot calendering" treatment, thereby realizing the continuous roll production of the polytetrafluoroethylene ceramic film;
2、与现有水性聚四氟乙烯陶瓷复合膜的生产工艺相比,本发明采用连续热压延的方法,逐渐提高材料密度,消除成膜缺陷,避免了现有水性乳液涂覆-烧结工艺带来的膜表面存在微孔、空洞等缺陷问题;制备的复合膜密度均匀,厚度均一,拉伸断裂强度优于现有水性乳液涂覆工艺生产的复合膜;2. Compared with the existing production process of water-based polytetrafluoroethylene ceramic composite membranes, the present invention adopts a continuous hot calendering method to gradually increase the material density, eliminate film-forming defects, and avoid the defects of micropores and voids on the membrane surface caused by the existing water-based emulsion coating-sintering process; the prepared composite membrane has uniform density and thickness, and its tensile strength is better than that of the composite membrane produced by the existing water-based emulsion coating process;
3、本发明所述方法可以获得具有高导热性能、高填料量的聚四氟乙烯陶瓷复合膜以及高导热的高频覆铜板材料;且具备高导热性和高频下的低介电损耗特性,适用于对热管理有较高要求的大功率高频高速印制线路板产品。3. The method of the present invention can obtain a polytetrafluoroethylene ceramic composite film with high thermal conductivity and high filler content and a high-frequency copper-clad laminate material with high thermal conductivity; and has high thermal conductivity and low dielectric loss characteristics at high frequencies, and is suitable for high-power, high-frequency, and high-speed printed circuit board products with high requirements for thermal management.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为实施例8制得的改性聚四氟乙烯及聚四氟乙烯的红外光谱测试结果。FIG. 1 is the infrared spectrum test results of modified polytetrafluoroethylene and polytetrafluoroethylene obtained in Example 8.
具体实施方式DETAILED DESCRIPTION
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.
使用原材料列表如下:The raw materials used are listed below:
日本大金,聚四氟乙烯树脂粉,牌号M-18F,粒径25μm。Japan Daikin, polytetrafluoroethylene resin powder, brand M-18F, particle size 25μm.
山东东岳,聚四氟乙烯悬浮细粉,牌号DF-162,粒径20-30μm。Shandong Dongyue, polytetrafluoroethylene suspension fine powder, brand DF-162, particle size 20-30μm.
美国3M公司,PFA树脂粉,牌号Dyneon PFA 6503PAZ,粒径30μm。3M Company, USA, PFA resin powder, brand name Dyneon PFA 6503PAZ, particle size 30μm.
美国3M公司,FEP树脂粉,牌号Dyneon FEP 6322PAZ,粒径5μm。3M Company, USA, FEP resin powder, brand name Dyneon FEP 6322PAZ, particle size 5μm.
江苏联瑞新材料股份有限公司,球形硅微粉,粒径2-4μm。Jiangsu Lianrui New Materials Co., Ltd., spherical silica powder, particle size 2-4μm.
山东国瓷,二氧化钛粉体,粒径1-10μm。Shandong National Ceramics, titanium dioxide powder, particle size 1-10μm.
陕西华特新材料,高硅氧玻璃短切纤维,直径0.9-3μm,长度定制。Shaanxi Walter New Materials, high silica glass chopped fibers, diameter 0.9-3μm, customizable length.
BYK公司,流变助剂,牌号RHEOBYK-410。BYK company, rheological additive, brand name RHEOBYK-410.
混合二甲苯,市售。Mixed xylene, commercially available.
埃克森美孚公司,芳烃溶剂,牌号Solvesso 100。ExxonMobil Corporation, aromatic solvent, brand Solvesso 100.
江苏华伦公司,芳烃溶剂,牌号Galasol S-100B。Jiangsu Hualun Company, aromatic solvent, brand name Galasol S-100B.
埃克森美孚公司,芳烃溶剂,牌号Solvesso 200ND。ExxonMobil, aromatic solvent, brand Solvesso 200ND.
江苏华伦公司,芳烃溶剂,牌号Galasol S-200。Jiangsu Hualun Company, aromatic solvent, brand name Galasol S-200.
本发明实施例购买得到的填料为硅烷偶联剂表面处理过的填料粉末。The filler purchased in the embodiment of the present invention is a filler powder surface-treated with a silane coupling agent.
实施例1Example 1
本实施例中,首先提供一种聚四氟乙烯陶瓷复合膜的制备方法,包括如下步骤:In this embodiment, a method for preparing a polytetrafluoroethylene ceramic composite membrane is first provided, comprising the following steps:
步骤1、将PTFE粉末(牌号M-18F)92重量份,PFA树脂粉8重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂20重量份,Solvesso 200ND芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液;Step 1, 92 parts by weight of PTFE powder (brand name M-18F), 8 parts by weight of PFA resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63 vol% of the total volume of fluororesin and filler), and stir and mix at high speed for 1 hour to obtain a uniformly dispersed emulsion;
步骤2、将上述胶液用卧式涂覆机涂覆在聚酰亚胺膜表面,烘箱分段温度为80、90、120、130、120℃,均速通过,总停留时间为3min,获得涂覆厚度为150μm的涂四氟乙烯胶PI膜;Step 2, the above glue solution is coated on the surface of the polyimide film by a horizontal coating machine, the oven segment temperature is 80, 90, 120, 130, 120 ° C, the speed is uniform, the total residence time is 3 minutes, and a tetrafluoroethylene glue-coated PI film with a coating thickness of 150 μm is obtained;
步骤3、将上述涂胶膜在连续热压机上进行放卷、热压、收卷,热压辊表面温度95℃,压延线速度为1.0m/min,压延辊顶压25t,通过热压操作,消除膜材料中的微孔,获得胶层厚度为140μm、复合PI膜的、含有高沸点芳烃溶剂的聚四氟乙烯陶瓷膜卷材;Step 3, unwinding, hot pressing, and winding the above-mentioned coated film on a continuous hot press, the surface temperature of the hot pressing roller is 95°C, the calendering line speed is 1.0m/min, the calendering roller top pressure is 25t, and the micropores in the membrane material are eliminated through the hot pressing operation to obtain a polytetrafluoroethylene ceramic membrane coil with a composite PI membrane and a high-boiling point aromatic solvent having a glue layer thickness of 140μm;
步骤4、将所述卷材通过通风烘箱,烘烤,挥发其中的高沸点溶剂;烘箱温度分段设置,五段温度为:220、240、260、260、220℃,均速通过,总停留时间7min;Step 4, passing the coil through a ventilated oven for baking to volatilize the high boiling point solvent therein; the oven temperature is set in stages, and the five temperatures are: 220, 240, 260, 260, 220°C, passing at an average speed, and the total residence time is 7 minutes;
步骤5、将步骤4处理后的卷材在连续热压机上,进行第二次热压处理,压辊表面温度110℃,压延线速度为1.5m/min,压延辊顶压25t,获得胶层厚度为127μm,复合PI膜的聚四氟乙烯陶瓷膜卷材;Step 5, subjecting the coiled material treated in step 4 to a second hot pressing treatment on a continuous hot press, with a roller surface temperature of 110° C., a calendering line speed of 1.5 m/min, and a calendering roller top pressure of 25 t, to obtain a polytetrafluoroethylene ceramic membrane coiled material with a composite PI membrane and a glue layer thickness of 127 μm;
步骤6、将步骤5所述卷材在高温烘箱中烧结,烧结温度350℃,时间10min,冷却后,剥离PI膜,收卷,制得聚四氟乙烯陶瓷复合膜卷材。Step 6: sinter the coiled material in step 5 in a high temperature oven at a sintering temperature of 350° C. for 10 min. After cooling, peel off the PI film and roll it up to obtain a polytetrafluoroethylene ceramic composite film coiled material.
本实施例中,还提供了一种聚四氟乙烯陶瓷基高频覆铜板的制备方法。In this embodiment, a method for preparing a polytetrafluoroethylene ceramic-based high-frequency copper-clad laminate is also provided.
将4张厚度为127μm的聚四氟乙烯陶瓷膜叠合,两面覆上厚度为1oz的铜箔,在真空热压机中进行连续层压。层压温度为380℃,层压压力为4.0MPa,最高温保持时间为2h,得到介质厚度为0.508mm的聚四氟乙烯陶瓷基高频覆铜板。Four 127μm thick polytetrafluoroethylene ceramic films were stacked, and both sides were covered with 1oz thick copper foil, and then continuously laminated in a vacuum hot press. The lamination temperature was 380℃, the lamination pressure was 4.0MPa, and the maximum temperature holding time was 2h, resulting in a polytetrafluoroethylene ceramic-based high-frequency copper-clad laminate with a dielectric thickness of 0.508mm.
实施例2Example 2
实施例2的制备步骤与实施例1相比,其中不同点在于,将PFA树脂粉替换为FEP树脂粉,即:The preparation steps of Example 2 are different from those of Example 1 in that the PFA resin powder is replaced with FEP resin powder, namely:
步骤1、将PTFE粉末(牌号M-18F)92重量份,FEP树脂粉8重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂20重量份,Solvesso 200ND芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液;Step 1, 92 parts by weight of PTFE powder (brand name M-18F), 8 parts by weight of FEP resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63 vol% of the total volume of fluororesin and filler), and stir and mix at high speed for 1 hour to obtain a uniformly dispersed emulsion;
其他步骤相同,制备得到127μm厚度聚四氟乙烯陶瓷复合膜卷材;制备得到0.508mm介质厚度聚四氟乙烯陶瓷基覆铜板。The other steps are the same, and a 127 μm thick polytetrafluoroethylene ceramic composite membrane coil is prepared; and a 0.508 mm medium thickness polytetrafluoroethylene ceramic-based copper-clad laminate is prepared.
实施例3Example 3
实施例3的制备步骤与实施例1相比,其中不同点在于,将PFA树脂粉替换为FEP树脂粉与PFA树脂粉1:1重量份的混合物,即:The preparation steps of Example 3 are different from those of Example 1, in that the PFA resin powder is replaced with a mixture of FEP resin powder and PFA resin powder in a ratio of 1:1 by weight, namely:
步骤1、将PTFE粉末(牌号M-18F)92重量份,PFA树脂粉4重量份,FEP树脂粉4重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂20重量份,Solvesso200ND芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液。Step 1, 92 parts by weight of PTFE powder (brand name M-18F), 4 parts by weight of PFA resin powder, 4 parts by weight of FEP resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63 vol% of the total volume of fluororesin and filler) are stirred and mixed at high speed for 1 hour to obtain a uniformly dispersed emulsion.
其他步骤相同,制备得到127μm厚度聚四氟乙烯陶瓷复合膜卷材;制备得到0.508mm介质厚度聚四氟乙烯陶瓷基覆铜板。The other steps are the same, and a 127 μm thick polytetrafluoroethylene ceramic composite membrane coil is prepared; and a 0.508 mm medium thickness polytetrafluoroethylene ceramic-based copper-clad laminate is prepared.
实施例4Example 4
实施例4的制备步骤与实施例1相比,其中不同点在于,氟树脂仅为PTFE树脂粉,即:The preparation steps of Example 4 are different from those of Example 1 in that the fluororesin is only PTFE resin powder, namely:
步骤1、将PTFE悬浮细粉(牌号DF-162)100重量份,流变助剂0.2重量份,混合二甲苯30重量份,GalasolS-100B芳烃溶剂20重量份,GalasolS-200芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液。Step 1. Mix 100 parts by weight of PTFE suspended fine powder (brand name DF-162), 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Galasol S-100B aromatic solvent, 10 parts by weight of Galasol S-200 aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63 vol% of the total volume of fluororesin and filler) with high-speed stirring for 1 hour to obtain a uniformly dispersed emulsion.
其他步骤相同,制备得到127μm厚度聚四氟乙烯陶瓷复合膜卷材;制备得到0.508mm介质厚度聚四氟乙烯陶瓷基覆铜板。The other steps are the same, and a 127 μm thick polytetrafluoroethylene ceramic composite membrane coil is prepared; and a 0.508 mm medium thickness polytetrafluoroethylene ceramic-based copper-clad laminate is prepared.
实施例5Example 5
本实施例中,提供一种厚度为63μm聚四氟乙烯陶瓷复合膜卷料的制备方法。In this embodiment, a method for preparing a polytetrafluoroethylene ceramic composite film roll with a thickness of 63 μm is provided.
步骤1、将PTFE粉末(牌号M-18F)92重量份,FEP树脂粉8重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂20重量份,Solvesso 200ND芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63vol%),进行高速搅拌混合0.5h,得到分散均匀的分散乳液,之后,将上述分散乳液加入球磨机中,冷却下高速球磨3h,得到分散均匀的细小颗粒乳液;Step 1, 92 parts by weight of PTFE powder (brand name M-18F), 8 parts by weight of FEP resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63 vol% of the total volume of fluororesin and filler), and stir and mix at high speed for 0.5 h to obtain a uniformly dispersed emulsion, then add the above-mentioned dispersed emulsion into a ball mill, and high-speed ball mill for 3 h under cooling to obtain a uniformly dispersed fine particle emulsion;
步骤2、将上述研磨后胶液用卧式涂覆机涂覆在聚酰亚胺膜表面,烘箱分段温度为80、90、120、130、120℃,均速通过,总停留时间为4min,获得涂覆厚度为75μm的涂四氟乙烯胶PI膜;Step 2, the above-mentioned ground glue liquid is coated on the surface of the polyimide film by a horizontal coating machine, the oven segment temperature is 80, 90, 120, 130, 120 ° C, the speed is uniform, the total residence time is 4 minutes, and a tetrafluoroethylene glue PI film with a coating thickness of 75 μm is obtained;
步骤3、将上述涂胶膜在连续热压机上进行放卷、热压、收卷,热压辊表面温度95℃,压延线速度为1.0 m/min,顶压30t。通过热压操作,消除膜材料中的微孔,获得胶层厚度为66μm、复合PI膜的、含有高沸点芳烃溶剂的聚四氟乙烯陶瓷膜卷材;Step 3: Unwind, hot press, and rewind the above-mentioned coated film on a continuous hot press, with the hot press roller surface temperature of 95°C, the calendering line speed of 1.0 m/min, and the top pressure of 30t. Through the hot press operation, the micropores in the membrane material are eliminated to obtain a polytetrafluoroethylene ceramic membrane coil with a composite PI membrane and a high-boiling-point aromatic solvent having a glue layer thickness of 66μm;
步骤4、将所述卷材通过通风烘箱,烘烤,挥发其中的高沸点溶剂。烘箱温度分段设置,五段温度为:220、240、260、260、220℃,均速通过,总停留时间7min;Step 4: Pass the coil through a ventilated oven to bake and volatilize the high boiling point solvent. The oven temperature is set in stages, with five stages of temperature: 220, 240, 260, 260, 220°C, with an average speed and a total residence time of 7 minutes;
步骤5、将步骤4处理后卷材在连续热压机上,进行第二次热压处理,热压辊表面温度120℃,压延线速度为1.5m/min,顶压35t,获得胶层厚度为63μm,复合PI膜的聚四氟乙烯陶瓷膜卷材;Step 5, subjecting the coiled material treated in step 4 to a second hot pressing treatment on a continuous hot pressing machine, with a hot pressing roller surface temperature of 120°C, a calendering line speed of 1.5m/min, and a top pressure of 35t, to obtain a polytetrafluoroethylene ceramic membrane coiled material with a composite PI membrane and a glue layer thickness of 63μm;
步骤6、所述卷材在高温烘箱中烧结,烧结温度350℃,时间30min,冷却后,剥离PI膜,收卷,制得聚四氟乙烯陶瓷复合膜卷材。Step 6: The coil is sintered in a high-temperature oven at a temperature of 350° C. for 30 min. After cooling, the PI film is peeled off and rolled up to obtain a polytetrafluoroethylene ceramic composite film coil.
本实施例中,还提供了一种聚四氟乙烯陶瓷基覆铜板的制备方法。In this embodiment, a method for preparing a polytetrafluoroethylene ceramic-based copper-clad laminate is also provided.
将4张厚度为63μm的聚四氟乙烯陶瓷膜叠合,两面覆上厚度为1/2oz的铜箔,在真空热压机中进行层压。层压温度为380℃,层压压力为4.0MPa,最高温保持时间为1h。得到介质厚度为0.25mm的聚四氟乙烯陶瓷基覆铜板。Four 63μm thick polytetrafluoroethylene ceramic films were stacked, and both sides were covered with 1/2oz thick copper foil, and laminated in a vacuum hot press. The lamination temperature was 380℃, the lamination pressure was 4.0MPa, and the maximum temperature holding time was 1h. A polytetrafluoroethylene ceramic-based copper-clad laminate with a dielectric thickness of 0.25mm was obtained.
实施例6Example 6
本实施例中,提供一种聚四氟乙烯陶瓷复合膜卷料的制备方法。In this embodiment, a method for preparing a polytetrafluoroethylene ceramic composite film roll is provided.
步骤1、将PTFE粉末(牌号M-18F)92重量份,PFA树脂粉8重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂20重量份,Solvesso 200ND芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的9.5vol%),二氧化钛微粉(二氧化钛微粉用量占氟树脂和填料总体积的40.5vol%),进行高速搅拌混合2h,得到分散均匀的分散乳液;Step 1, 92 parts by weight of PTFE powder (brand name M-18F), 8 parts by weight of PFA resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, spherical silica powder (the amount of spherical silica powder accounts for 9.5 vol% of the total volume of fluororesin and filler), titanium dioxide powder (the amount of titanium dioxide powder accounts for 40.5 vol% of the total volume of fluororesin and filler), and mix them at high speed for 2 hours to obtain a uniformly dispersed emulsion;
步骤2、将上述胶液用卧式涂覆机涂覆在铝箔表面,烘箱分段温度为80、90、120、130、120℃,均速通过,总停留时间为4min,获得涂覆厚度为125μm的涂四氟乙烯胶铝箔;Step 2, coating the above glue solution on the surface of aluminum foil by a horizontal coating machine, with the oven segment temperatures of 80, 90, 120, 130, and 120° C., passing through at an even speed, with a total residence time of 4 min, to obtain a polytetrafluoroethylene glue-coated aluminum foil with a coating thickness of 125 μm;
步骤3、将上述涂胶箔在续热压机上进行放卷、热压、收卷,热压辊表面温度100℃,压延线速度为1.0m/min,顶压25t,通过热压操作,消除膜材料中的微孔,获得胶层厚度为115μm、复合PI膜的、含有高沸点芳烃溶剂的聚四氟乙烯陶瓷膜卷材;Step 3, unwinding, hot pressing, and rewinding the above-mentioned coated foil on a hot press, the surface temperature of the hot pressing roller is 100° C., the calendering line speed is 1.0 m/min, and the top pressure is 25 t. Through the hot pressing operation, the micropores in the membrane material are eliminated to obtain a polytetrafluoroethylene ceramic membrane coil with a composite PI membrane and a high-boiling-point aromatic hydrocarbon solvent having a glue layer thickness of 115 μm;
步骤4、将所述卷材通过通风烘箱,烘烤,挥发其中的高沸点溶剂。烘箱温度分段设置,五段温度为:220、240、260、260、220℃,均速通过,总停留时间7min;Step 4: Pass the coil through a ventilated oven to bake and volatilize the high boiling point solvent. The oven temperature is set in stages, with five stages of temperature: 220, 240, 260, 260, 220°C, with an average speed and a total residence time of 7 minutes;
步骤5、将步骤4处理后卷材在连续热压机上,进行第二次热压处理,热压辊表面温度105℃,压延线速度为1.5m/min,顶压25t,获得胶层厚度为101μm的聚四氟乙烯陶瓷膜卷材;Step 5, subjecting the coiled material treated in step 4 to a second hot pressing treatment on a continuous hot pressing machine, with a hot pressing roller surface temperature of 105° C., a calendering line speed of 1.5 m/min, and a top pressure of 25 t, to obtain a polytetrafluoroethylene ceramic membrane coiled material with a glue layer thickness of 101 μm;
步骤6、所述卷材在高温烘箱中烧结,烧结温度350℃,时间10min,冷却后,剥离铝箔,收卷,制得所述聚四氟乙烯陶瓷复合膜卷材。Step 6: The coil is sintered in a high-temperature oven at a temperature of 350° C. for 10 min. After cooling, the aluminum foil is peeled off and the coil is rolled up to obtain the polytetrafluoroethylene ceramic composite membrane coil.
本实施例中,还提供了一种聚四氟乙烯陶瓷基覆铜板的制备方法。In this embodiment, a method for preparing a polytetrafluoroethylene ceramic-based copper-clad laminate is also provided.
将5张厚度为101μm的聚四氟乙烯陶瓷膜叠合,两面覆上厚度为1/2oz的铜箔,在真空热压机中进行层压。层压温度为370℃,层压压力为6.0MPa,最高温保持时间为1h。得到介质厚度为0.508 mm的聚四氟乙烯陶瓷基覆铜板。Five 101μm thick polytetrafluoroethylene ceramic films were stacked, and both sides were covered with 1/2oz thick copper foil, and laminated in a vacuum hot press. The lamination temperature was 370℃, the lamination pressure was 6.0MPa, and the maximum temperature holding time was 1h. A polytetrafluoroethylene ceramic-based copper-clad laminate with a dielectric thickness of 0.508 mm was obtained.
实施例7Example 7
本实施例中,提供一种短切玻纤增强的聚四氟乙烯复合膜卷料的制备方法。In this embodiment, a method for preparing a chopped glass fiber reinforced polytetrafluoroethylene composite film roll is provided.
步骤1、将PTFE粉末(牌号M-18F)90重量份,FEP树脂粉10重量份,流变助剂0.5重量份,混合二甲苯50重量份,Solvesso100芳烃溶剂30重量份,Solvesso 200ND芳烃溶10重量份,短切高硅氧玻璃纤维(长度小于3mm,短切高硅氧玻璃纤维用量占氟树脂和填料总体积的5vol%),进行高速分散混合2h,得到分散均匀的分散乳液;Step 1, 90 parts by weight of PTFE powder (brand name M-18F), 10 parts by weight of FEP resin powder, 0.5 parts by weight of rheological additive, 50 parts by weight of mixed xylene, 30 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, and short-cut high-silica glass fiber (length less than 3 mm, the amount of short-cut high-silica glass fiber accounts for 5 vol% of the total volume of fluororesin and filler), are dispersed and mixed at high speed for 2 hours to obtain a uniformly dispersed emulsion;
步骤2、将上述胶液用卧式涂覆机涂覆在铝箔表面,烘箱分段温度为80、90、120、130、120℃,均速通过,总停留时间为7min,获得涂覆厚度为135μm的涂四氟乙烯胶铝箔;Step 2, coating the above glue solution on the surface of aluminum foil by a horizontal coating machine, with the oven segment temperatures of 80, 90, 120, 130, and 120° C., passing through at an even speed, with a total residence time of 7 min, to obtain a polytetrafluoroethylene glue-coated aluminum foil with a coating thickness of 135 μm;
步骤3、将上述涂胶箔在续热压机上进行放卷、热压、收卷,热压辊表面温度100℃,线速度为1.0m/min,顶压25t,通过热压操作,消除膜材料中的微孔,获得胶层厚度为130μm、含有高沸点芳烃溶剂的玻纤增强聚四氟乙烯膜卷材;Step 3, unwinding, hot pressing, and rewinding the above-mentioned coated foil on a hot pressing machine, with the surface temperature of the hot pressing roller being 100° C., the line speed being 1.0 m/min, and the top pressure being 25 t. Through the hot pressing operation, micropores in the membrane material are eliminated to obtain a glass fiber reinforced polytetrafluoroethylene membrane coil with a glue layer thickness of 130 μm and containing a high-boiling point aromatic hydrocarbon solvent;
步骤4、将所述卷材通过通风烘箱,烘烤,挥发其中的高沸点溶剂。烘箱温度分段设置,五段温度为:220、240、260、260、220℃,均速通过,总停留时间7min;Step 4: Pass the coil through a ventilated oven to bake and volatilize the high boiling point solvent. The oven temperature is set in stages, with five stages of temperature: 220, 240, 260, 260, 220°C, with an average speed and a total residence time of 7 minutes;
步骤5、将步骤4处理后卷材在连续热压机上,进行第二次热压处理,热压辊表面温度120℃,压延线速度为1.5m/min,顶压25t,获得胶层厚度为127μm的短切玻纤增强聚四氟乙烯膜卷材;Step 5, subjecting the coiled material treated in step 4 to a second hot pressing treatment on a continuous hot pressing machine, with a hot pressing roller surface temperature of 120° C., a calendering line speed of 1.5 m/min, and a top pressure of 25 t, to obtain a chopped glass fiber reinforced polytetrafluoroethylene film coiled material with a glue layer thickness of 127 μm;
步骤6、所述卷材在高温烘箱中烧结,烧结温度350℃,时间10min,冷却后,剥离,收卷,制得所述短切随机玻纤增强聚四氟乙烯复合膜卷材。Step 6: The coil is sintered in a high-temperature oven at a temperature of 350° C. for 10 min. After cooling, the coil is peeled off and rolled up to obtain the chopped random glass fiber reinforced polytetrafluoroethylene composite film coil.
本实施例中,还提供了一种聚四氟乙烯陶瓷基覆铜板的制备方法。In this embodiment, a method for preparing a polytetrafluoroethylene ceramic-based copper-clad laminate is also provided.
将1张厚度为127μm的短切玻纤聚四氟乙烯膜,两面覆上厚度为1/2oz的铜箔,在真空热压机中进行层压。层压温度为380℃,层压压力为4.0MPa,最高温保持时间为1h。得到介质厚度为0.127mm的短切玻纤增强聚四氟乙烯基覆铜板。A 127μm thick chopped glass fiber polytetrafluoroethylene film was coated with 1/2oz thick copper foil on both sides and laminated in a vacuum hot press. The lamination temperature was 380℃, the lamination pressure was 4.0MPa, and the maximum temperature holding time was 1h. A chopped glass fiber reinforced polytetrafluoroethylene copper clad laminate with a dielectric thickness of 0.127mm was obtained.
实施例8Example 8
一种聚四氟乙烯陶瓷复合膜的制备方法与实施例1的区别:采用改性聚四氟乙烯替代聚四氟乙烯(PTFE粉末)。The difference between a method for preparing a polytetrafluoroethylene ceramic composite membrane and Example 1 is that modified polytetrafluoroethylene is used instead of polytetrafluoroethylene (PTFE powder).
一种聚四氟乙烯陶瓷基高频覆铜板的制备方法与实施例1的区别:采用本实施例制得的聚四氟乙烯陶瓷复合膜进行制备。The difference between a method for preparing a polytetrafluoroethylene ceramic-based high-frequency copper-clad laminate and Example 1 is that the polytetrafluoroethylene ceramic composite film prepared in this example is used for preparation.
改性聚四氟乙烯的制备方法,包括以下步骤:The preparation method of modified polytetrafluoroethylene comprises the following steps:
将聚四氟乙烯在60Co放射源中进行γ射线辐照48kGy,然后将辐照后的聚四氟乙烯加入到乙醇和蒸馏水的混合液中,再加入1-烯丙基乙内酰脲、硫酸亚铁铵和浓度为93wt%的浓硫酸,氮气氛围下,升温至68℃,反应6h,过滤,索氏抽提58h,干燥,获得改性聚四氟乙烯。上述聚四氟乙烯与混合液的质量体积比为1g:15mL;乙醇与蒸馏水的体积比为1:2;1-烯丙基乙内酰脲在混合液中的浓度为20wt%;硫酸亚铁铵在混合液中的浓度为0.08g/L;浓硫酸在混合液中的浓度为0.7mL/L。The polytetrafluoroethylene was irradiated with 48 kGy of gamma rays in a 60 Co radiation source, and then the irradiated polytetrafluoroethylene was added to a mixture of ethanol and distilled water, and then 1-allylhydantoin, ammonium ferrous sulfate and concentrated sulfuric acid with a concentration of 93 wt% were added, and the temperature was raised to 68°C under a nitrogen atmosphere, reacted for 6 hours, filtered, Soxhlet extracted for 58 hours, and dried to obtain modified polytetrafluoroethylene. The mass volume ratio of the above polytetrafluoroethylene to the mixed solution is 1 g: 15 mL; the volume ratio of ethanol to distilled water is 1: 2; the concentration of 1-allylhydantoin in the mixed solution is 20 wt%; the concentration of ammonium ferrous sulfate in the mixed solution is 0.08 g/L; and the concentration of concentrated sulfuric acid in the mixed solution is 0.7 mL/L.
对上述制得的改性聚四氟乙烯及聚四氟乙烯进行红外光谱测试,结果如图1所示。由图1可知,与聚四氟乙烯的红外谱图相比,改性聚四氟乙烯的红外谱图在1663cm-1处存在C=O键的红外特征吸收峰,在1573cm-1处存在N-H键的红外特征吸收峰,说明1-烯丙基乙内酰脲参与了改性聚四氟乙烯的生成反应。The modified polytetrafluoroethylene and polytetrafluoroethylene prepared above were subjected to infrared spectrum test, and the results are shown in Figure 1. As shown in Figure 1, compared with the infrared spectrum of polytetrafluoroethylene, the infrared spectrum of modified polytetrafluoroethylene has an infrared characteristic absorption peak of C=O bond at 1663cm -1 and an infrared characteristic absorption peak of NH bond at 1573cm -1 , indicating that 1-allylhydantoin participates in the formation reaction of modified polytetrafluoroethylene.
实施例1-8中制得的聚四氟乙烯陶瓷复合膜卷材,厚度均匀,表观致密,具有足够的拉伸强度和撕裂强度,可在机械设备上进行收卷、放卷、裁切等操作。实施例1-8所制备的覆铜板,尺寸18英寸乘以24英寸,同一批次抽取10张测试,按照IPC-TM-650有关高频覆铜板标准测试方法,测试其介质厚度,厚度公差,介电常数、介电损耗,CTE。The polytetrafluoroethylene ceramic composite film coils prepared in Examples 1-8 have uniform thickness, dense appearance, sufficient tensile strength and tear strength, and can be rolled, unrolled, cut, etc. on mechanical equipment. The copper clad laminates prepared in Examples 1-8 have a size of 18 inches by 24 inches. Ten sheets are taken from the same batch for testing. According to the IPC-TM-650 standard test method for high-frequency copper clad laminates, the dielectric thickness, thickness tolerance, dielectric constant, dielectric loss, and CTE are tested.
表1实施例1-8制备的覆铜板的性能测试结果Table 1 Performance test results of copper clad laminates prepared in Examples 1-8
从表1中可以看出,实施例1-8所制备覆铜板,具备厚度均一性好,介电损耗低于0.0030,热膨胀系数低等优点,可用于高频高速线路板。It can be seen from Table 1 that the copper clad laminates prepared in Examples 1-8 have the advantages of good thickness uniformity, dielectric loss less than 0.0030, low thermal expansion coefficient, etc., and can be used for high-frequency and high-speed circuit boards.
通过实施例5可知,本发明所述技术可涂出最低厚度达60μm的均匀陶瓷膜,且性能与127μm的陶瓷膜压合出的高频板性能无差异。It can be seen from Example 5 that the technology described in the present invention can coat a uniform ceramic film with a minimum thickness of 60 μm, and the performance is no different from that of a high-frequency board pressed with a 127 μm ceramic film.
通过实施例6可知,本发明所述技术可以通过改变填料种类和加入量,制备高介电常数的聚四氟乙烯覆铜板。It can be seen from Example 6 that the technology described in the present invention can prepare a polytetrafluoroethylene copper clad laminate with a high dielectric constant by changing the type and amount of filler added.
通过实施例7可知,本发明所述技术也可适用于纤维状填料。通过加入少量的短切纤维,可以获得介电常数为2.20左右的高频覆铜板。且与纯PTFE片状材料相比较(热膨胀系数为230-250ppm/℃),实施例7所制备的覆铜板z轴热膨胀系数明显减小。It can be seen from Example 7 that the technology described in the present invention can also be applied to fibrous fillers. By adding a small amount of chopped fibers, a high-frequency copper-clad laminate with a dielectric constant of about 2.20 can be obtained. Compared with pure PTFE sheet material (thermal expansion coefficient of 230-250ppm/℃), the z-axis thermal expansion coefficient of the copper-clad laminate prepared in Example 7 is significantly reduced.
对于实施例1-4及实施例8获得的聚四氟乙烯陶瓷膜,测试了其相对密度、拉伸性能,通过显微镜观察了其表面的形貌。The relative density and tensile properties of the polytetrafluoroethylene ceramic membranes obtained in Examples 1-4 and Example 8 were tested, and their surface morphologies were observed under a microscope.
表2实施例1-4及实施例8获得的聚四氟乙烯陶瓷膜的性能测试结果Table 2 Performance test results of polytetrafluoroethylene ceramic membranes obtained in Examples 1-4 and Example 8
从表2的结果可知,实施例1-3中含有一定量的FEP树脂和PFA树脂,相比实施例4而言,由于FEP树脂和PFA树脂的流动性,陶瓷膜的密度略高,拉伸强度较好,表观形貌表现更好。因此,一定量的FEP树脂或PFA树脂对于陶瓷膜的力学性能改善和表观缺陷改善是有正面作用的。所制备的覆铜板的基本性能也无显著差异。From the results in Table 2, it can be seen that Examples 1-3 contain a certain amount of FEP resin and PFA resin. Compared with Example 4, due to the fluidity of FEP resin and PFA resin, the density of the ceramic film is slightly higher, the tensile strength is better, and the surface morphology is better. Therefore, a certain amount of FEP resin or PFA resin has a positive effect on improving the mechanical properties and surface defects of the ceramic film. There is no significant difference in the basic properties of the prepared copper clad laminate.
另外,由表2可知,实施例8与实施例1相比,密度及拉伸强度均有所提升,说明采用改性聚四氟乙烯替代聚四氟乙烯制备得到的陶瓷复合膜具有良好的密度及拉伸强度。In addition, it can be seen from Table 2 that compared with Example 1, the density and tensile strength of Example 8 are improved, indicating that the ceramic composite membrane prepared by using modified polytetrafluoroethylene instead of polytetrafluoroethylene has good density and tensile strength.
对比例1Comparative Example 1
对比例1的制备步骤与实施例1相比,其中不同点在于,PFA树脂粉末的添加量为30重量份,PTFE粉末添加量为70重量份,即:The preparation steps of Comparative Example 1 are compared with those of Example 1, wherein the addition amount of PFA resin powder is 30 parts by weight, and the addition amount of PTFE powder is 70 parts by weight, namely:
步骤1、将PTFE粉末(牌号M-18F)70重量份,PFA树脂粉30重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂20重量份,Solvesso 200ND芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63.1vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液。Step 1: 70 parts by weight of PTFE powder (brand name M-18F), 30 parts by weight of PFA resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63.1 vol% of the total volume of fluororesin and filler) are mixed at high speed for 1 hour to obtain a uniformly dispersed emulsion.
其他步骤相同,制备得到127μm厚度聚四氟乙烯陶瓷复合膜卷材;制备得到0.508mm介质厚度聚四氟乙烯陶瓷基覆铜板。The other steps are the same, and a 127 μm thick polytetrafluoroethylene ceramic composite membrane coil is prepared; and a 0.508 mm medium thickness polytetrafluoroethylene ceramic-based copper-clad laminate is prepared.
对比例1中获得的覆铜板,按照IPC-TM-650有关高频覆铜板标准测试方法,测试其介电常数、介电损耗,CTE。The copper clad laminate obtained in Comparative Example 1 was tested for its dielectric constant, dielectric loss, and CTE according to the standard test method for high-frequency copper clad laminates in IPC-TM-650.
表3 对比例1获得的覆铜板的性能测试结果Table 3 Performance test results of copper clad laminate obtained in Comparative Example 1
通过将实施例1-4与对比例1相比较,由表3可知,如果PFA的加入量过高,所制备出的覆铜板介电损耗会明显增加。而介电常数和热膨胀系数无明显变化。说明PFA或FEP树脂粉有较优加入量的上限。经过实验验证,本发明所述方案中,优选地,以所有氟树脂粉末重量为100份,聚四氟乙烯树脂粉末的重量不低于85份。By comparing Examples 1-4 with Comparative Example 1, it can be seen from Table 3 that if the amount of PFA added is too high, the dielectric loss of the prepared copper clad laminate will increase significantly. However, there is no significant change in the dielectric constant and the thermal expansion coefficient. This indicates that there is an upper limit to the amount of PFA or FEP resin powder added. After experimental verification, in the scheme described in the present invention, preferably, the weight of the polytetrafluoroethylene resin powder is not less than 85 parts based on 100 parts by weight of all fluororesin powders.
对比例2Comparative Example 2
本对比例中采用水性聚四氟乙烯乳液制备聚四氟乙烯陶瓷膜和覆铜板。In this comparative example, aqueous polytetrafluoroethylene emulsion was used to prepare polytetrafluoroethylene ceramic membrane and copper clad laminate.
本对比例中采用的原材料如下:The raw materials used in this comparative example are as follows:
聚四氟乙烯浓缩水乳液,牌号DF-304,固含量60wt%;Polytetrafluoroethylene concentrated aqueous emulsion, brand DF-304, solid content 60wt%;
FEP水乳液,牌号ND-4R,固含量39%;FEP water emulsion, brand ND-4R, solid content 39%;
球形硅微粉,粒径2-4μm;Spherical silica powder, particle size 2-4μm;
RHEOBYK-7600水性增稠剂,15%水溶液。RHEOBYK-7600 water-based thickener, 15% aqueous solution.
本对比例的制备步骤如下:The preparation steps of this comparative example are as follows:
取上述聚四氟乙烯水乳液150重量份,FEP水乳液25.6重量份,增稠剂1.0重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63.2vol%),混合2h,后加入去离子水,调节粘度至700mPa•s,得到聚四氟乙烯陶瓷复合水性浆料。Take 150 parts by weight of the above-mentioned polytetrafluoroethylene aqueous emulsion, 25.6 parts by weight of FEP aqueous emulsion, 1.0 part by weight of thickener, and spherical silica powder (the amount of spherical silica powder accounts for 63.2 vol% of the total volume of fluororesin and filler), mix for 2 hours, then add deionized water and adjust the viscosity to 700 mPa•s to obtain a polytetrafluoroethylene ceramic composite aqueous slurry.
将浆料进行卧式涂覆,涂覆在聚酰亚胺基膜表面,烘箱温度分段设置85℃,获得涂覆厚度为130μm的涂四氟乙烯陶瓷PI膜。将获得的生膜,在高温隧道式通风烘箱中预烧,排出有机小分子物,烘箱温度分段设置260℃。随后,高温烘箱中350℃下烧结15min,成为致密的聚四氟乙烯陶瓷复合薄膜。最后,冷却后,将PI膜剥离,获得厚度为127μm聚四氟乙烯陶瓷复合膜卷材。The slurry is horizontally coated on the surface of the polyimide base film, and the oven temperature is set at 85°C in stages to obtain a 130μm thick polytetrafluoroethylene ceramic PI film. The obtained raw film is pre-burned in a high-temperature tunnel ventilation oven to discharge small organic molecules, and the oven temperature is set at 260°C in stages. Subsequently, it is sintered at 350°C in a high-temperature oven for 15 minutes to form a dense polytetrafluoroethylene ceramic composite film. Finally, after cooling, the PI film is peeled off to obtain a polytetrafluoroethylene ceramic composite film coil with a thickness of 127μm.
将上述4张厚度为127μm的聚四氟乙烯陶瓷膜叠合,两面覆上厚度为1oz的铜箔,在真空热压机中进行层压。层压温度为380℃,层压压力为4.0MPa,最高温保持时间为2h。得到介质厚度为0.508 mm的聚四氟乙烯陶瓷基覆铜板。The above four 127μm thick polytetrafluoroethylene ceramic films were stacked, and both sides were covered with 1oz thick copper foil, and laminated in a vacuum hot press. The lamination temperature was 380℃, the lamination pressure was 4.0MPa, and the maximum temperature holding time was 2h. A polytetrafluoroethylene ceramic-based copper-clad laminate with a dielectric thickness of 0.508 mm was obtained.
对于对比例2所获得的聚四氟乙烯陶瓷膜,测试了其相对密度、拉伸性能,通过显微镜观察了其表面的形貌。The relative density and tensile properties of the polytetrafluoroethylene ceramic membrane obtained in Comparative Example 2 were tested, and its surface morphology was observed under a microscope.
表4 对比例2获得的聚四氟乙烯陶瓷膜的性能测试结果Table 4 Performance test results of polytetrafluoroethylene ceramic membrane obtained in Comparative Example 2
通过将实施例1-4与对比例2相比较,由表4可知,采用水相乳液制备的聚四氟乙烯陶瓷膜,相对密度小,表观缺陷明显增加。由于表面缺陷多,水相法获得的陶瓷膜拉伸强度低,断裂伸长率也有所下降。因此,实际操作中,水相浆料涂覆-烧结法获得的聚四氟乙烯陶瓷膜卷料在收卷、放卷和裁切操作时,需要小心轻放,控制张力,避免撕裂。By comparing Examples 1-4 with Comparative Example 2, it can be seen from Table 4 that the polytetrafluoroethylene ceramic membrane prepared by the aqueous emulsion has a low relative density and a significant increase in apparent defects. Due to the large number of surface defects, the ceramic membrane obtained by the aqueous method has a low tensile strength and a reduced elongation at break. Therefore, in actual operation, the polytetrafluoroethylene ceramic membrane coil obtained by the aqueous slurry coating-sintering method needs to be carefully handled during winding, unwinding and cutting operations to control tension and avoid tearing.
对比例2所制备的覆铜板,尺寸18英寸乘以24英寸,同一批次抽取10张测试,按照IPC-TM-650有关高频覆铜板标准测试方法,测试其介质厚度,厚度公差,介电常数、介电损耗,CTE。The copper clad laminate prepared in Comparative Example 2 has a size of 18 inches by 24 inches. Ten sheets are selected from the same batch for testing. According to the IPC-TM-650 standard test method for high-frequency copper clad laminates, the dielectric thickness, thickness tolerance, dielectric constant, dielectric loss, and CTE are tested.
表5 对比例2制备的覆铜板的性能测试结果Table 5 Performance test results of copper clad laminate prepared in Comparative Example 2
通过将实施例1-4制备的覆铜板与对比例2相比较,由表5可知,由于对比例2所制备的水性乳液在连续涂覆的过程薄膜厚度控制较差,前后生产的薄膜材料在热压成覆铜板后厚度相差较大,制备的同一批次材料的介质厚度公差较大。此外,由于对比例2制备的薄膜存在微观缺陷,材料的介电常数有所降低,介电损耗略高。By comparing the copper clad laminates prepared in Examples 1-4 with Comparative Example 2, it can be seen from Table 5 that due to the poor film thickness control of the aqueous emulsion prepared in Comparative Example 2 during the continuous coating process, the thickness of the film materials produced before and after are greatly different after being hot-pressed into copper clad laminates, and the dielectric thickness tolerance of the same batch of materials prepared is large. In addition, due to the presence of microscopic defects in the film prepared in Comparative Example 2, the dielectric constant of the material is reduced and the dielectric loss is slightly higher.
由此可见,本发明所述技术方案,与目前已报道的水性乳液涂覆技术方案相比,可以有效消除成膜缺陷,避免了现有工艺存在微孔、空洞等缺陷问题;制备的复合膜厚度均一性好;拉伸断裂强度优于水性乳液涂覆工艺。It can be seen that the technical solution described in the present invention can effectively eliminate film-forming defects and avoid defects such as micropores and voids in the existing process compared with the currently reported water-based emulsion coating technical solution; the prepared composite film has good thickness uniformity; and the tensile breaking strength is better than the water-based emulsion coating process.
对比例3Comparative Example 3
对比例3中,在浆料中不加入高沸点芳烃溶剂,尝试制备所述聚四氟乙烯膜。In Comparative Example 3, the polytetrafluoroethylene membrane was attempted to be prepared without adding a high-boiling point aromatic hydrocarbon solvent to the slurry.
步骤1、将PTFE粉末(牌号M-18F)92重量份,PFA树脂粉8重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂30重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63.2vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液;Step 1, 92 parts by weight of PTFE powder (brand name M-18F), 8 parts by weight of PFA resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 30 parts by weight of Solvesso 100 aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63.2 vol% of the total volume of fluororesin and filler), are stirred and mixed at high speed for 1 hour to obtain a uniformly dispersed emulsion;
步骤2、将上述胶液用卧式涂覆机涂覆在聚酰亚胺膜表面,烘箱分段温度为80、90、120、130、120℃,均速通过,总停留时间为3min,获得涂覆厚度为135μm的涂四氟乙烯胶PI膜;Step 2, the above glue solution is coated on the surface of the polyimide film by a horizontal coating machine, the oven segment temperature is 80, 90, 120, 130, 120 ° C, the speed is uniform, the total residence time is 3 minutes, and a tetrafluoroethylene glue-coated PI film with a coating thickness of 135 μm is obtained;
步骤3、将上述涂胶膜在连续热压延机上进行放卷、热压、收卷,热压辊表面温度95℃,压延线速度1.0m/min,顶压25t;Step 3, unwinding, hot pressing and winding the above-mentioned adhesive film on a continuous hot calender, the surface temperature of the hot pressing roller is 95°C, the calendering line speed is 1.0m/min, and the top pressure is 25t;
步骤4、将所述卷材通过通风烘箱,烘烤,温度设置260℃,停留时间7min;Step 4: pass the coil through a ventilated oven for baking at a temperature of 260° C. for a residence time of 7 min;
步骤5、所述卷材在高温烘箱中烧结,烧结温度350℃,时间10min,冷却后,尝试剥离PI膜,获得聚四氟乙烯陶瓷膜。Step 5: The coil is sintered in a high-temperature oven at a temperature of 350° C. for 10 min. After cooling, the PI film is peeled off to obtain a polytetrafluoroethylene ceramic film.
对比例3中制备得到的聚四氟乙烯陶瓷膜,表面裂纹多,强度较差。在步骤5中,难以完整地从PI基膜表面剥离。由对比例3可知,本发明所述方法中,高沸点芳烃溶剂是必须的,特别是高/低沸点芳烃组合溶剂的配合设置并形成分步挥发。聚四氟乙烯溶剂型乳液的单一“涂覆-烘烤-烧结”工艺,无法获得表面致密的聚四氟乙烯陶瓷膜卷料。The polytetrafluoroethylene ceramic membrane prepared in Comparative Example 3 has many surface cracks and poor strength. In step 5, it is difficult to completely peel off from the surface of the PI base film. As can be seen from Comparative Example 3, in the method of the present invention, a high-boiling point aromatic hydrocarbon solvent is necessary, especially the combination of high/low boiling point aromatic hydrocarbon solvents and the formation of step-by-step volatilization. The single "coating-baking-sintering" process of polytetrafluoroethylene solvent-based emulsion cannot obtain a polytetrafluoroethylene ceramic membrane roll with a dense surface.
对比例4Comparative Example 4
对比例4中,与实施例1相比较,去掉步骤3与步骤5所述的热压延操作,尝试制备聚四氟乙烯膜。In Comparative Example 4, compared with Example 1, the hot calendering operations described in Step 3 and Step 5 were removed to attempt to prepare a polytetrafluoroethylene film.
步骤1、将PTFE粉末(牌号M-18F)92重量份,PFA树脂粉8重量份,流变助剂0.2重量份,混合二甲苯30重量份,Solvesso 100芳烃溶剂20重量份,Solvesso 200ND芳烃溶剂10重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的63.2vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液;Step 1, 92 parts by weight of PTFE powder (brand name M-18F), 8 parts by weight of PFA resin powder, 0.2 parts by weight of rheological additive, 30 parts by weight of mixed xylene, 20 parts by weight of Solvesso 100 aromatic solvent, 10 parts by weight of Solvesso 200ND aromatic solvent, and spherical silica powder (the amount of spherical silica powder accounts for 63.2 vol% of the total volume of fluororesin and filler), and stir and mix at high speed for 1 hour to obtain a uniformly dispersed emulsion;
步骤2、将上述胶液用卧式涂覆机涂覆在聚酰亚胺膜表面,烘箱分段温度为80、90、120、130、120℃,均速通过,总停留时间为3min,获得涂覆厚度为150μm的涂四氟乙烯胶PI膜;Step 2, the above glue solution is coated on the surface of the polyimide film by a horizontal coating machine, the oven segment temperature is 80, 90, 120, 130, 120 ° C, the speed is uniform, the total residence time is 3 minutes, and a tetrafluoroethylene glue-coated PI film with a coating thickness of 150 μm is obtained;
步骤3、将所述卷材通过通风烘箱,烘烤,挥发其中的高沸点溶剂。烘箱温度分段设置,五段温度为:220、240、260、260、220℃,均速通过,总停留时间7min;Step 3: Pass the coil through a ventilated oven to bake and volatilize the high boiling point solvent. The oven temperature is set in stages, with five stages of temperature: 220, 240, 260, 260, 220°C, with an average speed and a total residence time of 7 minutes;
步骤4、所述卷材在高温烘箱中烧结,烧结温度350℃,时间10min,冷却后,尝试剥离PI膜,获得聚四氟乙烯陶瓷复合膜。Step 4: the coil is sintered in a high temperature oven at a temperature of 350° C. for 10 min. After cooling, the PI film is peeled off to obtain a polytetrafluoroethylene ceramic composite film.
对于对比例4所获得的聚四氟乙烯陶瓷膜,测试了其相对密度、拉伸性能,观察了其表面的形貌。For the polytetrafluoroethylene ceramic membrane obtained in Comparative Example 4, its relative density and tensile properties were tested, and its surface morphology was observed.
表6 对比例4获得的聚四氟乙烯陶瓷膜的性能测试结果Table 6 Performance test results of polytetrafluoroethylene ceramic membrane obtained in Comparative Example 4
由表6可知,对比例4中制备得到的聚四氟乙烯陶瓷膜,表面存在肉眼可见裂纹,薄膜强度较差,步骤4难以成卷。由上表的结果可知,与实施例1-4对比,对比例4所制备薄膜无连续热压延步骤,密度极大降低,拉伸强度低,表观缺陷明显。说明本发明所述连续热压延步骤是必要的,尤其是分步连续热压延。As shown in Table 6, the polytetrafluoroethylene ceramic film prepared in Comparative Example 4 has visible cracks on the surface, the film strength is poor, and it is difficult to roll in step 4. As shown in the results of the above table, compared with Examples 1-4, the film prepared in Comparative Example 4 has no continuous hot calendering step, the density is greatly reduced, the tensile strength is low, and the apparent defects are obvious. This shows that the continuous hot calendering step of the present invention is necessary, especially the step-by-step continuous hot calendering.
实施例9Embodiment 9
实施例9提供了一种高导热聚四氟乙烯基覆铜板的制备方法。Example 9 provides a method for preparing a high thermal conductivity polytetrafluoroethylene-based copper clad laminate.
本实施例与之前实施例所不同的原材料列表如下:The raw materials that are different between this embodiment and the previous embodiment are listed as follows:
球形氧化铝,型号BAK5,粒径D50=5-6μm;Spherical alumina, model BAK5, particle size D50 = 5-6 μm;
类球形氧化铝,型号NSM-1S,粒径D50=0.8μm;Quasi-spherical alumina, model NSM-1S, particle size D50 = 0.8 μm;
球形氮化硼,型号GBN-60,粒径D50=60-75μm;Spherical boron nitride, model GBN-60, particle size D50 = 60-75μm;
片状氮化硼,型号ABN-15,粒径D50=12-13μm。Flake boron nitride, model ABN-15, particle size D50=12-13μm.
高导热聚四氟乙烯陶瓷膜的制备方法如下:The preparation method of high thermal conductivity polytetrafluoroethylene ceramic film is as follows:
步骤1、步骤1、将PTFE粉末(牌号M-18F)90重量份,FEP树脂粉10重量份,流变助剂0.5重量份,混合二甲苯60重量份,Solvesso 100芳烃溶剂40重量份,Solvesso 200ND芳烃溶剂20重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的19vol%),球形氮化硼(球形氮化硼用量占氟树脂和填料总体积的12vol%),片状氮化硼(片状氮化硼用量占氟树脂和填料总体积的9.5vol%),氧化铝(氧化铝用量占氟树脂和填料总体积的19.5vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液;Step 1: 90 parts by weight of PTFE powder (brand name M-18F), 10 parts by weight of FEP resin powder, 0.5 parts by weight of rheological additive, 60 parts by weight of mixed xylene, 40 parts by weight of Solvesso 100 aromatic solvent, 20 parts by weight of Solvesso 200ND aromatic solvent, spherical silica powder (the amount of spherical silica powder accounts for 19 vol% of the total volume of fluororesin and filler), spherical boron nitride (the amount of spherical boron nitride accounts for 12 vol% of the total volume of fluororesin and filler), flaky boron nitride (the amount of flaky boron nitride accounts for 9.5 vol% of the total volume of fluororesin and filler), and alumina (the amount of alumina accounts for 19.5 vol% of the total volume of fluororesin and filler) are mixed under high-speed stirring for 1 hour to obtain a uniformly dispersed emulsion;
步骤2、将上述胶液用卧式涂覆机涂覆在聚酰亚胺膜表面,烘箱分段温度为80、100、120、130、120℃,均速通过,总停留时间为5min,获得涂覆厚度为150μm的涂四氟乙烯胶PI膜;Step 2, the above glue solution is coated on the surface of the polyimide film by a horizontal coating machine, the oven segment temperature is 80, 100, 120, 130, 120 ° C, the speed is uniform, the total residence time is 5 minutes, and a tetrafluoroethylene glue-coated PI film with a coating thickness of 150 μm is obtained;
步骤3、将上述涂胶膜在续热压机上进行放卷、热压、收卷,热压辊表面温度95℃,压延线速度1.5m/min,顶压25 t,通过热压操作,消除膜材料中的微孔,获得胶层厚度为140μm、复合PI膜的、含有高沸点芳烃溶剂的聚四氟乙烯陶瓷膜卷材;Step 3, unwinding, hot pressing, and winding the above-mentioned coated film on a hot pressing machine, the surface temperature of the hot pressing roller is 95° C., the calendering line speed is 1.5 m/min, and the top pressure is 25 t. Through the hot pressing operation, the micropores in the membrane material are eliminated to obtain a polytetrafluoroethylene ceramic membrane coil with a composite PI membrane and a high-boiling point aromatic solvent having a glue layer thickness of 140 μm;
步骤4、将所述卷材通过通风烘箱,烘烤,挥发其中的高沸点溶剂。烘箱温度分段设置,五段温度为:220、240、260、260、220℃,均速通过,总停留时间7min;Step 4: Pass the coil through a ventilated oven to bake and volatilize the high boiling point solvent. The oven temperature is set in stages, with five stages of temperature: 220, 240, 260, 260, 220°C, with an average speed and a total residence time of 7 minutes;
步骤5、将步骤4处理后卷材在连续热压机上,进行第二次热压处理,热压辊表面温度110℃,顶压35 t,获得胶层厚度为127μm,复合PI膜的聚四氟乙烯陶瓷膜卷材;Step 5, subjecting the coiled material treated in step 4 to a second hot pressing treatment on a continuous hot pressing machine, with the surface temperature of the hot pressing roller being 110° C. and the top pressure being 35 t, to obtain a polytetrafluoroethylene ceramic membrane coiled material with a composite PI membrane and a glue layer thickness of 127 μm;
步骤6、所述卷材在高温烘箱中烧结,烧结温度350℃,时间10min,冷却后,剥离PI膜,收卷,制得所述聚四氟乙烯陶瓷复合膜卷材。Step 6: The coil is sintered in a high-temperature oven at a sintering temperature of 350° C. for 10 min. After cooling, the PI film is peeled off and rolled up to obtain the polytetrafluoroethylene ceramic composite membrane coil.
本实施例中,提供了一种聚四氟乙烯陶瓷基覆铜板的制备方法。In this embodiment, a method for preparing a polytetrafluoroethylene ceramic-based copper-clad laminate is provided.
将4张厚度为127μm的聚四氟乙烯陶瓷膜叠合,两面覆上厚度为1oz的铜箔,在真空热压机中进行层压。层压温度为380℃,层压压力为7.0MPa,最高温保持时间为2h。得到介质厚度为0.508mm的高导热聚四氟乙烯陶瓷基覆铜板。Four 127μm thick polytetrafluoroethylene ceramic films were stacked, and both sides were covered with 1oz thick copper foil, and laminated in a vacuum hot press. The lamination temperature was 380℃, the lamination pressure was 7.0MPa, and the maximum temperature holding time was 2h. A high thermal conductivity polytetrafluoroethylene ceramic-based copper-clad laminate with a dielectric thickness of 0.508mm was obtained.
实施例10Example 10
与实施例9相比,实施例10中改变了氧化铝、氮化硼导热填料的比例,如下所示。Compared with Example 9, the ratio of alumina and boron nitride thermal conductive fillers is changed in Example 10, as shown below.
步骤1、将PTFE粉末(牌号M-18F)90重量份,FEP树脂粉10重量份,流变助剂0.5重量份,混合二甲苯60重量份,Solvesso 100芳烃溶剂40重量份,Solvesso 200ND芳烃溶剂20重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的30vol%),球形氮化硼(球形氮化硼用量占氟树脂和填料总体积的20vol%),片状氮化硼(片状氮化硼用量占氟树脂和填料总体积的10vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液;Step 1, 90 parts by weight of PTFE powder (brand name M-18F), 10 parts by weight of FEP resin powder, 0.5 parts by weight of rheological additive, 60 parts by weight of mixed xylene, 40 parts by weight of Solvesso 100 aromatic solvent, 20 parts by weight of Solvesso 200ND aromatic solvent, spherical silica powder (the amount of spherical silica powder accounts for 30 vol% of the total volume of fluororesin and filler), spherical boron nitride (the amount of spherical boron nitride accounts for 20 vol% of the total volume of fluororesin and filler), and flake boron nitride (the amount of flake boron nitride accounts for 10 vol% of the total volume of fluororesin and filler), and stir and mix at high speed for 1 hour to obtain a uniformly dispersed emulsion;
其他步骤与实施例9相同。制备得到介质厚度为0.508mm高导热聚四氟乙烯陶瓷基覆铜板。The other steps are the same as those in Example 9. A high thermal conductivity polytetrafluoroethylene ceramic-based copper-clad laminate with a dielectric thickness of 0.508 mm is prepared.
对比例5Comparative Example 5
与实施例9相比,对比例5中,制备了对比例5a,对比例5b,对比例5c种不同导热填料的体积加入量的样品,总调料体积比率(即导热填料占氟树脂和填料总体积的比率)分别为30vol%、40vol%,75vol%,更改后配比如表7所示:Compared with Example 9, in Comparative Example 5, samples with different volume addition amounts of thermally conductive fillers were prepared in Comparative Example 5a, Comparative Example 5b, and Comparative Example 5c, and the total volume ratio of the seasoning (i.e., the ratio of the thermally conductive filler to the total volume of the fluororesin and the filler) was 30 vol%, 40 vol%, and 75 vol%, respectively. The modified proportions are shown in Table 7:
其他步骤1中的配比与步骤实施与实施例9相同。制备得到3种介质厚度为0.508mm高导热聚四氟乙烯陶瓷基覆铜板。The other proportions and steps in step 1 are the same as those in Example 9. Three kinds of high thermal conductivity polytetrafluoroethylene ceramic-based copper-clad laminates with a dielectric thickness of 0.508 mm were prepared.
表7 实施例9与对比例5a,对比例5b及对比例5c的配比量Table 7 The proportions of Example 9 and Comparative Example 5a, Comparative Example 5b and Comparative Example 5c
对比例6Comparative Example 6
与实施例9相比,对比例6中只采用高填充量的氧化铝,未加入氮化硼、二氧化硅填料,如下所示。Compared with Example 9, Comparative Example 6 only uses a high amount of aluminum oxide without adding boron nitride and silicon dioxide fillers, as shown below.
步骤1、将PTFE粉末(牌号M-18F)90重量份,FEP树脂粉10重量份,流变助剂1.0重量份,混合二甲苯70重量份,Solvesso 100芳烃溶剂50重量份,Solvesso 200ND芳烃溶剂20重量份,球形氧化铝填料(球形氧化铝用量占氟树脂和填料总体积的70vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液。Step 1: 90 parts by weight of PTFE powder (brand name M-18F), 10 parts by weight of FEP resin powder, 1.0 parts by weight of rheological additive, 70 parts by weight of mixed xylene, 50 parts by weight of Solvesso 100 aromatic solvent, 20 parts by weight of Solvesso 200ND aromatic solvent, and spherical alumina filler (the amount of spherical alumina accounts for 70 vol% of the total volume of fluororesin and filler) are mixed at high speed for 1 hour to obtain a uniformly dispersed emulsion.
其他步骤与实施例9相同。制备得到介质厚度为0.508mm高导热聚四氟乙烯陶瓷基覆铜板。The other steps are the same as those in Example 9. A high thermal conductivity polytetrafluoroethylene ceramic-based copper-clad laminate with a dielectric thickness of 0.508 mm is prepared.
对比例7Comparative Example 7
与实施例9相比,对比例7中未采用球形氮化硼填料,而将其中球形氮化硼全部替换成片状氮化硼填料,具体步骤如下所示:Compared with Example 9, Comparative Example 7 does not use spherical boron nitride fillers, but replaces all spherical boron nitride fillers with flake boron nitride fillers. The specific steps are as follows:
步骤1、将PTFE粉末(牌号M-18F)90重量份,FEP树脂粉10重量份,流变助剂0.5重量份,混合二甲苯60重量份,Solvesso100芳烃溶剂40重量份,Solvesso 200ND芳烃溶剂20重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的19vol%),片状氮化硼(片状氮化硼用量占氟树脂和填料总体积的21.5vol%),氧化铝(氧化铝用量占氟树脂和填料总体积的19.5vol%),进行高速搅拌混合1h,得到分散均匀的分散乳液;Step 1, 90 parts by weight of PTFE powder (brand name M-18F), 10 parts by weight of FEP resin powder, 0.5 parts by weight of rheological additive, 60 parts by weight of mixed xylene, 40 parts by weight of Solvesso 100 aromatic solvent, 20 parts by weight of Solvesso 200ND aromatic solvent, spherical silica powder (the amount of spherical silica powder accounts for 19 vol% of the total volume of fluororesin and filler), flaky boron nitride (the amount of flaky boron nitride accounts for 21.5 vol% of the total volume of fluororesin and filler), and alumina (the amount of alumina accounts for 19.5 vol% of the total volume of fluororesin and filler), and mixing at high speed for 1 hour to obtain a uniformly dispersed emulsion;
其他步骤与实施例9相同。制备得到介质厚度为0.508mm高导热聚四氟乙烯陶瓷基覆铜板。The other steps are the same as those in Example 9. A high thermal conductivity polytetrafluoroethylene ceramic-based copper-clad laminate with a dielectric thickness of 0.508 mm is prepared.
对于上述实施例9-10,对比例5-7制作的覆铜板,测试其介电常数,介电损耗和导热性能。The dielectric constant, dielectric loss and thermal conductivity of the copper clad laminates prepared in the above-mentioned Examples 9-10 and Comparative Examples 5-7 were tested.
表8 实施例9-10、对比例5-7制作的覆铜板的性能测试结果Table 8 Performance test results of copper clad laminates prepared in Examples 9-10 and Comparative Examples 5-7
通过实施例9、10可以看到,本发明提供的技术方案可以制备导热系数不小于1.2W/(m•K)的高导热聚四氟乙烯基高频板。通过对氧化铝、氮化硼、二氧化硅的比例、数量调节,可制备介电常数为3.00-3.50左右的覆铜板材料。其损耗也满足高频板要求。It can be seen from Examples 9 and 10 that the technical solution provided by the present invention can prepare a high thermal conductivity polytetrafluoroethylene-based high-frequency board with a thermal conductivity coefficient of not less than 1.2W/(m•K). By adjusting the ratio and quantity of aluminum oxide, boron nitride, and silicon dioxide, a copper-clad board material with a dielectric constant of about 3.00-3.50 can be prepared. Its loss also meets the requirements of high-frequency boards.
通过实施例9与对比例5a、5b、5c的导热率比较,说明随着同样比例填料体积百分比的增加(30vol%-75vol%),导热率呈现先增大后减少的趋势。当填料体积比较低时,导热填料间形成的通路较少,复合材料导热率较低;当填料体积比过大时,导热填料间的空气间隙急剧增加,复合材料导热率下降。经过试验验证,采用本发明中所述导热填料和聚四氟乙烯树脂体系,填料总的体积比为50vol%至70vol%之间。优选的,为55vol%至65vol%之间。By comparing the thermal conductivity of Example 9 with that of Comparative Examples 5a, 5b, and 5c, it is shown that with the increase in the volume percentage of the same proportion of fillers (30vol%-75vol%), the thermal conductivity shows a trend of first increasing and then decreasing. When the filler volume ratio is relatively low, fewer passages are formed between the thermally conductive fillers, and the thermal conductivity of the composite material is low; when the filler volume ratio is too large, the air gap between the thermally conductive fillers increases sharply, and the thermal conductivity of the composite material decreases. After experimental verification, using the thermally conductive filler and polytetrafluoroethylene resin system described in the present invention, the total volume ratio of the filler is between 50vol% and 70vol%. Preferably, it is between 55vol% and 65vol%.
对比例6不采用氮化硼,仅仅加入球形氧化铝作为导热填料。即使在较高的导热填料的添加量下,对比例6中复合材料的导热率为0.85W/(m•K)。通过实施例9与对比例6的导热率比较,说明要实现本发明所设定的导热率目标值,氮化硼填料的加入是必须的。Comparative Example 6 does not use boron nitride, but only adds spherical alumina as a thermally conductive filler. Even at a relatively high addition amount of thermally conductive filler, the thermal conductivity of the composite material in Comparative Example 6 is 0.85 W/(m•K). By comparing the thermal conductivity of Example 9 with that of Comparative Example 6, it is shown that the addition of boron nitride filler is necessary to achieve the target thermal conductivity value set by the present invention.
对比例7将所有球形氮化硼替换为同质量的片状氮化硼,与实施例9相比,导热系数显著降低,说明球形氮化硼填料的加入对复合材料的导热率提升明显。因此,本发明中所述球形氮化硼填料加入是必须的。In Comparative Example 7, all spherical boron nitrides are replaced with flake boron nitrides of the same mass. Compared with Example 9, the thermal conductivity is significantly reduced, indicating that the addition of spherical boron nitride fillers significantly improves the thermal conductivity of the composite material. Therefore, the addition of spherical boron nitride fillers in the present invention is necessary.
对比例8Comparative Example 8
与实施例9相比较,本对比例尝试采用水性聚四氟乙烯乳液制备高导热聚四氟乙烯陶瓷膜和覆铜板。Compared with Example 9, this comparative example attempts to use an aqueous polytetrafluoroethylene emulsion to prepare a high thermal conductivity polytetrafluoroethylene ceramic film and a copper clad laminate.
本对比例的制备步骤如下:The preparation steps of this comparative example are as follows:
取聚四氟乙烯水乳液150份,FEP水乳液25.6重量份,水性增稠剂1.0重量份,球形硅微粉(球形硅微粉用量占氟树脂和填料总体积的19vol%),球形氮化硼(用量占氟树脂和填料总体积的12vol%),片状氮化硼(用量占氟树脂和填料总体积的9.5vol%),氧化铝(用量占氟树脂和填料总体积的19.5vol%),混合2h,后加入去离子水,调节粘度至1000mPa•s,得到含导热填料的聚四氟乙烯陶瓷复合水性浆料;Take 150 parts of polytetrafluoroethylene aqueous emulsion, 25.6 parts by weight of FEP aqueous emulsion, 1.0 parts by weight of aqueous thickener, spherical silica powder (the amount of spherical silica powder accounts for 19 vol% of the total volume of fluororesin and filler), spherical boron nitride (the amount accounts for 12 vol% of the total volume of fluororesin and filler), flaky boron nitride (the amount accounts for 9.5 vol% of the total volume of fluororesin and filler), and alumina (the amount accounts for 19.5 vol% of the total volume of fluororesin and filler), mix for 2 hours, then add deionized water, adjust the viscosity to 1000 mPa•s, and obtain a polytetrafluoroethylene ceramic composite aqueous slurry containing thermal conductive filler;
将浆料进行卧式涂覆,涂覆在聚酰亚胺基膜表面,烘箱温度两段设置80、100℃,均速通过,总停留时间5min,获得涂覆厚度为130μm的涂四氟乙烯陶瓷PI膜。然后,在260℃的通风烘箱中烘烤。由于烘烤后材料开裂严重,强度过低,部分区域填料出现分离现象,无法进一步成型。The slurry was horizontally coated on the surface of the polyimide base film, and the oven temperature was set at 80 and 100 ° C in two stages, with an average speed and a total residence time of 5 minutes to obtain a 130 μm thick tetrafluoroethylene ceramic PI film. Then, it was baked in a ventilated oven at 260 ° C. Due to severe cracking of the material after baking, the strength was too low, and the filler in some areas was separated, and further molding could not be performed.
通过对比例8可知,采用现有的水性聚四氟乙烯乳液“涂覆-烧结”工艺难以制备含有高体积比(60vol%)的高导热填料的聚四氟乙烯陶瓷。It can be seen from Comparative Example 8 that it is difficult to prepare polytetrafluoroethylene ceramics containing a high volume ratio (60 vol%) of high thermal conductive filler using the existing aqueous polytetrafluoroethylene emulsion "coating-sintering" process.
以上所述仅为本发明的优选实施例,并非因此限制本发明的专利范围,凡是在本发明的发明构思下,利用本发明说明书及附图内容所作的等效结构变换,或直接/间接运用在其他相关的技术领域均包括在本发明的专利保护范围内。The above description is only a preferred embodiment of the present invention, and does not limit the patent scope of the present invention. All equivalent structural changes made by using the contents of the present invention specification and drawings under the inventive concept of the present invention, or directly/indirectly applied in other related technical fields are included in the patent protection scope of the present invention.
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