TWI601582B - Method for producing raw material for papermaking, raw material for papermaking obtained, and heat-resistant electrical insulating sheet using the same - Google Patents
Method for producing raw material for papermaking, raw material for papermaking obtained, and heat-resistant electrical insulating sheet using the same Download PDFInfo
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- TWI601582B TWI601582B TW102148386A TW102148386A TWI601582B TW I601582 B TWI601582 B TW I601582B TW 102148386 A TW102148386 A TW 102148386A TW 102148386 A TW102148386 A TW 102148386A TW I601582 B TWI601582 B TW I601582B
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- raw material
- pressure jet
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- 239000002994 raw material Substances 0.000 title claims description 31
- 238000004519 manufacturing process Methods 0.000 title claims description 18
- 239000000835 fiber Substances 0.000 claims description 58
- 239000002245 particle Substances 0.000 claims description 39
- 238000003490 calendering Methods 0.000 claims description 22
- 238000009826 distribution Methods 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 10
- 125000003118 aryl group Chemical group 0.000 claims description 6
- 229920000768 polyamine Polymers 0.000 claims description 5
- 230000014759 maintenance of location Effects 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims 4
- 239000000123 paper Substances 0.000 description 63
- 238000000034 method Methods 0.000 description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000007788 liquid Substances 0.000 description 7
- -1 poly(phenylene isophthalamide) Polymers 0.000 description 7
- 239000002002 slurry Substances 0.000 description 7
- 238000010009 beating Methods 0.000 description 6
- 238000010292 electrical insulation Methods 0.000 description 6
- 238000002156 mixing Methods 0.000 description 6
- 239000002184 metal Substances 0.000 description 5
- 230000035699 permeability Effects 0.000 description 5
- 229920000412 polyarylene Polymers 0.000 description 5
- 238000010298 pulverizing process Methods 0.000 description 5
- VZXTWGWHSMCWGA-UHFFFAOYSA-N 1,3,5-triazine-2,4-diamine Chemical compound NC1=NC=NC(N)=N1 VZXTWGWHSMCWGA-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- 150000001412 amines Chemical class 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 239000003623 enhancer Substances 0.000 description 4
- 238000007731 hot pressing Methods 0.000 description 4
- 239000002609 medium Substances 0.000 description 4
- 229920000877 Melamine resin Polymers 0.000 description 3
- 229920000784 Nomex Polymers 0.000 description 3
- 239000002518 antifoaming agent Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 3
- 239000004763 nomex Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 2
- 239000004760 aramid Substances 0.000 description 2
- 229920003235 aromatic polyamide Polymers 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000007580 dry-mixing Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000003365 glass fiber Substances 0.000 description 2
- QZUPTXGVPYNUIT-UHFFFAOYSA-N isophthalamide Chemical compound NC(=O)C1=CC=CC(C(N)=O)=C1 QZUPTXGVPYNUIT-UHFFFAOYSA-N 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 229920000962 poly(amidoamine) Polymers 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- WZCQRUWWHSTZEM-UHFFFAOYSA-N 1,3-phenylenediamine Chemical compound NC1=CC=CC(N)=C1 WZCQRUWWHSTZEM-UHFFFAOYSA-N 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 238000012695 Interfacial polymerization Methods 0.000 description 1
- 239000004696 Poly ether ether ketone Substances 0.000 description 1
- 229920000265 Polyparaphenylene Polymers 0.000 description 1
- 239000004734 Polyphenylene sulfide Substances 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 229920003367 Teijinconex Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000012736 aqueous medium Substances 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 238000000149 argon plasma sintering Methods 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- GFAUNYMRSKVDJL-UHFFFAOYSA-N formyl chloride Chemical compound ClC=O GFAUNYMRSKVDJL-UHFFFAOYSA-N 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012761 high-performance material Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 229940018564 m-phenylenediamine Drugs 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000011490 mineral wool Substances 0.000 description 1
- 239000011268 mixed slurry Substances 0.000 description 1
- 230000004660 morphological change Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- 229920003207 poly(ethylene-2,6-naphthalate) Polymers 0.000 description 1
- 229920000767 polyaniline Polymers 0.000 description 1
- 229920002530 polyetherether ketone Polymers 0.000 description 1
- 239000011112 polyethylene naphthalate Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920000069 polyphenylene sulfide Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000004765 teijinconex Substances 0.000 description 1
- MHSKRLJMQQNJNC-UHFFFAOYSA-N terephthalamide Chemical compound NC(=O)C1=CC=C(C(N)=O)C=C1 MHSKRLJMQQNJNC-UHFFFAOYSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
- D21B1/32—Defibrating by other means of waste paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/10—Organic non-cellulose fibres
- D21H13/20—Organic non-cellulose fibres from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H13/26—Polyamides; Polyimides
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/52—Addition to the formed paper by contacting paper with a device carrying the material
- D21H23/56—Rolls
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Paper (AREA)
- Physics & Mathematics (AREA)
- Spectroscopy & Molecular Physics (AREA)
Description
本發明係關於一種經砑光加工之聚芳醯胺紙的再利用方法及一種耐熱性電絕緣片材。詳言之,本發明係關於一種在不使用藥液的情況下,即可使原採用以焚燒或廢棄方式處理的經砑光加工之聚芳醯胺紙再生的一種經砑光加工之聚芳醯胺紙的再利用方法,以及一種耐熱性電絕緣片材。 The present invention relates to a method for recycling a calendered polyaramide paper and a heat resistant electrical insulating sheet. In particular, the present invention relates to a calendered polyaryl that can be regenerated by calendering or polyaniline paper which has been treated by incineration or disposal without the use of a chemical solution. A method of recycling a guanamine paper, and a heat-resistant electrically insulating sheet.
目前已有人開發出一種以高性能材料所製造、故具有較佳強度及/或熱穩定性的紙。例如聚芳醯胺紙,此係由芳香族聚醯胺所形成的合成紙,由於具有優異的耐熱性、耐燃性、電絕緣性、強韌性及可撓性,而可作為電絕緣材料及用於飛機之蜂巢結構的基材。這樣的材料也包含杜邦(DuPont)(美國)的Nomex(註冊商標)纖維所形成的紙,其係以下述方式製作:將聚(間伸苯基間苯二甲醯胺)(poly(metaphenylene isophthalamide))短纖維與纖條體(fibrid)在水中混合,接著對混合之漿液進行抄紙,再進行砑光加工。目前已知這種紙在高溫下依然具有高強度及強韌性,同時具有優異的電絕緣性。 Papers have been developed which are made of high performance materials and therefore have better strength and/or thermal stability. For example, polyarsenin paper, which is a synthetic paper made of aromatic polyamine, can be used as an electrical insulating material because of its excellent heat resistance, flame resistance, electrical insulation, toughness and flexibility. The substrate of the honeycomb structure of the aircraft. Such materials also include paper formed by DuPont (USA) Nomex (registered trademark) fibers, which are produced in the following manner: poly(metaphenylene isophthalamide) (poly(metaphenylene isophthalamide)) )) The short fibers and the fibrid are mixed in water, and then the mixed slurry is subjected to papermaking, followed by calendering. It is currently known that such papers still have high strength and toughness at high temperatures, and have excellent electrical insulation properties.
由於聚芳醯胺紙經過砑光加工之高溫高壓處理,只用水無法完全將其廢料及破損材料等原纖化(fibrillated),所以必須進行焚燒或廢棄 處理。又,亦可在溶解於有機溶劑後,實施化學再生而使其形成與初始原料相同的抄紙原料,即短纖維及纖條體、紙漿等,但該方法需考量環境因素,且成本可能會變高。 Due to the high temperature and high pressure treatment of the melamine paper, the waste and the damaged material cannot be completely fibrillated by water, so it must be incinerated or discarded. deal with. Further, after being dissolved in an organic solvent, chemical regeneration may be carried out to form a papermaking raw material similar to the initial raw material, that is, short fibers, fibrids, pulp, etc., but the method requires consideration of environmental factors, and the cost may vary. high.
又,專利文獻1及2中記載的處理方法係關於對未實施砑光加工之高溫高壓處理的乾燥聚芳醯胺紙或是聚芳醯胺紙板的再生方法。然而,聚芳醯胺紙實際上大多是在經過砑光加工後使用,故該等方法並不實用。 Further, the processing methods described in Patent Documents 1 and 2 are related to a method for regenerating dry polyarylamide paper or polyarylimine paperboard which is subjected to high temperature and high pressure treatment which is not subjected to calendering. However, polyarylamide papers are mostly used after calendering, so these methods are not practical.
更進一步言之,專利文獻3中記載之方法,係使用將聚芳醯胺紙粉碎後所形成的聚芳醯胺紙漿,與非聚芳醯胺系纖維以90/10~10/90質量比進行混合抄紙形成片狀後,用以製造多孔性聚芳醯胺成形物,但因該成形物為多孔性,一般認為其電絕緣性不佳。 Furthermore, the method described in Patent Document 3 uses a polyarsenide pulp which is formed by pulverizing a polyarylamine paper, and a mass ratio of 90/10 to 10/90 with a non-polyarsenamide fiber. After the mixed papermaking is formed into a sheet shape, the porous polyamidamine molded article is produced. However, since the molded article is porous, it is generally considered to have poor electrical insulating properties.
【專利文獻1】日本特開平4-228696號公報 [Patent Document 1] Japanese Patent Laid-Open No. 4-228696
【專利文獻2】日本特開2003-290676號公報 [Patent Document 2] Japanese Patent Laid-Open Publication No. 2003-290676
【專利文獻3】日本特開平7-243189號公報 [Patent Document 3] Japanese Patent Laid-Open No. Hei 7-243189
本發明之目的在於提供一種抄紙用原料之製造方法,可在不使用藥液的情況下,將經研光加工之聚芳醯胺紙碎裂成可再利用的抄紙用原料,而以之作為抄紙用原料。 An object of the present invention is to provide a method for producing a raw material for papermaking, which is capable of disintegrating a light-processed polyarylamide paper into a reusable raw material for papermaking without using a chemical liquid. Raw materials for papermaking.
本發明之另一目的在於提供一種由經砑光加工之聚芳醯胺紙所製得的抄紙用原料。 Another object of the present invention is to provide a raw material for papermaking which is obtained from calendered polyaramide paper.
本發明之另一目的在於提供一種耐熱性電絕緣片材,其使用上述抄紙用原料。 Another object of the present invention is to provide a heat-resistant electrically insulating sheet which uses the above-mentioned raw material for papermaking.
本發明係基於下述發現而完成:若對經砑光加工所製造之特定的聚芳醯胺紙進行高壓噴射處理而使其碎裂,則可得到具有優異特性且可再生之抄紙用原料。 The present invention has been accomplished on the basis of the following findings: When a specific polyaramide paper produced by calendering is subjected to high-pressure jet treatment to be broken, a raw material for papermaking having excellent characteristics and recyclable can be obtained.
亦即,本發明提供一種抄紙用原料之製造方法,其特徵在於:將由芳香族聚醯胺所形成之纖條體、短纖維、或其混合物所形成、並經砑光加工所製造的聚芳醯胺紙進行高壓噴射處理而使其碎裂聚芳醯胺紙。 That is, the present invention provides a method for producing a raw material for papermaking, which comprises a fibril formed from an aromatic polyamine, a short fiber, or a mixture thereof, and is produced by calendering. The guanamine paper is subjected to high pressure jet treatment to break up the polyamidamide paper.
本發明又提供一種抄紙用原料,其係以上述製造方法製得。 The present invention further provides a raw material for papermaking which is obtained by the above production method.
本發明又提供一種耐熱性電絕緣片材,其特徵在於:包含上述抄紙用原料。 The present invention further provides a heat-resistant electrically insulating sheet comprising the above-mentioned raw material for papermaking.
(聚芳醯胺,aramid) (polyarylamine, aramid)
在本發明中,聚芳醯胺係指60%以上的醯胺鍵直接與芳香環鍵結的線狀高分子化合物(芳香族聚醯胺)。這樣的聚芳醯胺係如:聚間伸苯基間苯二甲醯胺及其共聚物、聚對伸苯基對苯二甲醯胺(polyparaphenylene terephthalamide)及其共聚物、聚(對伸苯基)-共聚(3,4-二苯基醚)對苯二甲醯胺(poly(paraphenylene)-copoly(3,4diphenylether)terephthalamide)等。該等聚芳醯胺可藉由下列方式取得,例如使用間苯二 甲酸氯化物及間苯二胺的習知界面聚合法、溶液聚合法等來進行工業上的製造,亦可由市售品取得,但並不限定於此。從具有良好的成型加工性、熱黏合性、阻燃性、耐熱性等特性的觀點來看,該等聚芳醯胺中較佳為使用聚間伸苯基間苯二甲醯胺。 In the present invention, polyarsenamide refers to a linear polymer compound (aromatic polyamine) in which 60% or more of a guanamine bond is directly bonded to an aromatic ring. Such polyarylamines are, for example, poly(phenylene isophthalamide) and copolymers thereof, polyparaphenylene terephthalamide and copolymers thereof, and poly(p-phenylene) ())-(3,4-diphenyl ether) poly(paraphenylene)-copoly(3,4diphenylether) terephthalamide or the like. The polyarylamines can be obtained by, for example, using isophthalic acid Commercially produced by a conventional interfacial polymerization method, a solution polymerization method, or the like of a formic acid chloride or m-phenylenediamine, and may be obtained from a commercially available product, but is not limited thereto. From the viewpoint of having characteristics such as good moldability, thermal adhesiveness, flame retardancy, heat resistance and the like, it is preferred to use poly(m-phenylene phthalamide) among the polyarylamines.
(聚芳醯胺纖條體) (polyarylamine fibrid)
在本發明中,聚芳醯胺纖條體,係具有抄紙性之薄膜狀醯胺粒子,亦稱為聚芳醯胺紙漿(aramid pulp)(參照日本特公昭35-11851號公報、日本特公昭37-5732號公報等)。 In the present invention, the polyarylamine fibrids are paper-like guanamine particles having a papermaking property, which is also called aramid pulp (refer to Japanese Patent Publication No. 35-11851, Japanese Special Public Sho. Bulletin No. 37-5732, etc.).
目前已知,聚芳醯胺纖條體可與一般的木材紙漿相同地實施分解、打漿處理,而作為抄紙原料;可對其實施為了保持適合抄紙之品質的打漿處理。該打漿處理可藉由碟狀磨漿設備、打漿設備及其他可發揮機械性切斷作用的抄紙原料處理設備來實施。在該操作中,可用日本工業規格(JIS)P8121所規定的遊離度試驗方法(freeness test)來監控纖條體之形態變化。在本發明中,實施打漿處理後之聚芳醯胺纖條體的遊離度較佳為在10cm3~300cm3(加拿大遊離度)的範圍內。以遊離度之範圍大於該範圍的纖條體所形成之耐熱性電絕緣片材的強度可能會降低。另一方面,若遊離度小於10cm3,多會發生輸入機械動力的使用效率變小、且每單位時間之處理量變少的情況;更進一步來說,纖條體過度地微細化容易使黏著功能降低。因此,並不認為遊離度小於10cm3具有特別的優點。 It is known that polyarsenide fibrids can be subjected to decomposition and beating treatment in the same manner as general wood pulp, and can be used as a papermaking raw material; it can be subjected to a beating treatment for maintaining the quality suitable for papermaking. The beating treatment can be carried out by a disc refining apparatus, a beating apparatus, and other papermaking raw material processing equipment capable of exerting a mechanical cutting action. In this operation, the morphological change of the fibrids can be monitored by the freeness test prescribed by Japanese Industrial Standards (JIS) P8121. In the present invention, the freeness of the polyarylamine fibrids after the beating treatment is preferably in the range of 10 cm 3 to 300 cm 3 (Canadian freeness). The strength of the heat-resistant electrically insulating sheet formed by the fibrids having a range of freeness larger than the range may be lowered. On the other hand, when the degree of freeness is less than 10 cm 3 , the use efficiency of the input mechanical power is reduced, and the amount of treatment per unit time is reduced. Further, the fibrid body is excessively fined to facilitate the adhesion function. reduce. Therefore, it is not considered that the freeness is less than 10 cm 3 has a particular advantage.
(聚芳醯胺短纖維) (polyarsenamide short fiber)
聚芳醯胺短纖維以聚芳醯胺作為材料的纖維切斷。這種纖維係如:帝人股份有限公司的「TEIJIN CONEX(註冊商標)」、杜邦公司的 「NOMEX(註冊商標)」等,但並不限定於此。 The polyarylamine short fibers are cut with fibers of polyarmine amine as a material. This type of fiber is such as: "TEIJIN CONEX (registered trademark)" of Teijin Co., Ltd., DuPont "NOMEX (registered trademark)", etc., but is not limited to this.
聚芳醯胺短纖維的長度一般係選自1mm以上、未達50mm的範圍,較佳係選自2~10mm的範圍。若短纖維的長度小於1mm,則片材的力學特性降低;另外,若其長度在50mm以上,則在以濕式法製造聚芳醯胺紙時,容易發生「糾結」、「纏繞成束」等情況,而容易成為造成缺陷的原因。 The length of the polyarylamine short fibers is generally selected from the range of 1 mm or more and less than 50 mm, and is preferably selected from the range of 2 to 10 mm. When the length of the short fibers is less than 1 mm, the mechanical properties of the sheet are lowered. Further, when the length is 50 mm or more, when the polyamidamide paper is produced by a wet method, "tangling" and "winding into bundles" are likely to occur. Waiting for the situation, it is easy to become the cause of the defect.
(聚芳醯胺紙) (polyarylamine paper)
在本發明中,聚芳醯胺紙係主要由前述聚芳醯胺纖條體、聚芳醯胺短纖維、或其混合物所構成的片狀物,一般而言,其厚度係在20μm~1000μm的範圍內。更進一步言之,聚芳醯胺紙一般的基重係在10g/m2~1000g/m2的範圍內。 In the present invention, the polyarylamine paper is a sheet mainly composed of the above-mentioned polyarylamine fibrids, polyarsenamide short fibers, or a mixture thereof, and generally has a thickness of 20 μm to 1000 μm. In the range. Furthermore, polyarylamine papers generally have a basis weight in the range of 10 g/m 2 to 1000 g/m 2 .
一般來說,聚芳醯胺紙係以將上述聚芳醯胺纖條體與聚芳醯胺短纖維混合後再將其薄片化的方法來製造。具體而言,可使用下列方法:如將上述聚芳醯胺纖條體及聚芳醯胺短纖維進行乾式混合後,利用氣流形成薄片的方法;將聚芳醯胺纖條體及聚芳醯胺短纖維在液體介質中分散混合後,投至具有液體通透性的支持體(例如網或帶)上而將其薄片化,再去除液體以將其乾燥的方法等;在前述方法中,較佳係選擇以水作為介質的所謂濕式製造法。在這裡,聚芳醯胺纖條體與聚芳醯胺短纖維可以任意比例混合,但聚芳醯胺纖條體/聚芳醯胺短纖維的比例(質量比)較佳為1/9~9/1,更佳為2/8~8/2。 In general, polyaramide paper is produced by mixing the above-mentioned polyarylamine fibrids and polyarmine light fibers and then flaking them. Specifically, the following methods can be used: a method of forming a sheet by air flow after dry mixing of the above-mentioned polyarylamine fibrids and polyarsenamide short fibers; and polyarylene fibril and polyarylene a method in which an amine short fiber is dispersed and mixed in a liquid medium, and then poured onto a support having a liquid permeability (for example, a mesh or a belt) to be flaky, and then the liquid is removed to dry it; in the foregoing method, It is preferred to select a so-called wet manufacturing method using water as a medium. Here, the polyarylamine fibrids and the polyarylamine short fibers may be mixed in any ratio, but the ratio (mass ratio) of the polyarylamine fibrids/polyarsenamide short fibers is preferably 1/9~ 9/1, more preferably 2/8~8/2.
在濕式製造法中,一般係將至少含有聚芳醯胺纖條體、聚芳醯胺短纖維之單一種類或其混合物的水性漿液供給至抄紙機以使其分散之後,進行脫水、擠水及乾燥步驟,以得出片材而將其捲繞起來。抄紙機可 利用長網抄紙機、圓網抄紙機、傾斜型抄紙機及將該等裝置組合得出的混合抄紙機等。在以混合抄紙機進行製造的情況下,可使摻合比例不同的漿液形成薄片並合為一體,而得到由複數紙層所形成的複合薄片。在進行抄紙時,如有必要,可使用分散性提升劑、消泡劑、紙力增強劑等添加劑。 In the wet manufacturing method, an aqueous slurry containing at least a polyaminin fibrid, a single species of polyarmine amine short fibers or a mixture thereof is supplied to a paper machine to be dispersed, and then dehydrated and squeezed. And a drying step to obtain a sheet and wind it up. Paper machine A long-wire paper machine, a rotary paper machine, a tilting paper machine, and a hybrid paper machine obtained by combining the same. In the case of production by a hybrid paper machine, the slurry having different blending ratios can be formed into a sheet and integrated to obtain a composite sheet formed of a plurality of paper layers. When performing papermaking, if necessary, additives such as a dispersibility enhancer, an antifoaming agent, and a paper strength enhancer may be used.
(砑光加工) (砑光加工)
目前已知,將上述方法所得之聚芳醯胺紙在一對滾筒之間以高溫高壓進行熱壓後,除可提高其密度、結晶化程度、耐熱性、尺寸穩定性以外,亦可提升機械強度。例如,在使用金屬製滾筒的情況下,例示的熱壓條件雖為溫度在100~350℃、線壓在50~400kg/cm的範圍內,但並不限定於此。熱壓時亦可堆疊複數聚芳醯胺紙來進行。上述熱壓加工亦可以任意順序進行多次。 It is known that the polyaramide paper obtained by the above method can be heated under high temperature and high pressure between a pair of rollers, and the density, crystallization degree, heat resistance and dimensional stability can be improved, and the machine can be lifted. strength. For example, in the case of using a metal drum, the hot pressing conditions exemplified are a temperature of 100 to 350 ° C and a linear pressure of 50 to 400 kg/cm, but are not limited thereto. When hot pressing, a plurality of polyamido papers may be stacked. The above hot press processing can also be performed multiple times in any order.
(高壓噴射處理) (high pressure jet treatment)
在本發明中,高壓噴射處理係指如下所述的處理:將上述經砑光加工之聚芳醯胺紙浸漬於水中,並與水一同從噴嘴高壓噴射,以使其撞擊衝撞用硬物,或使高壓噴射之上述經砑光加工的聚芳醯胺紙彼此相互撞擊,而使上述經砑光加工之聚芳醯胺紙碎裂,進而形成與聚芳醯胺纖條體及聚芳醯胺短纖維相似的形狀。 In the present invention, the high-pressure jet treatment refers to a treatment in which the above-mentioned calendered polyaramide paper is immersed in water and sprayed with water from a nozzle at a high pressure to cause it to collide with a hard object for collision. Or causing the high-pressure jetting of the above-mentioned calendered polyarsenamide paper to collide with each other, thereby disintegrating the above-mentioned calendered polyarylamide paper to form polyarylamine fibrids and polyarylene A similar shape of the amine staple fiber.
較佳係使用高壓均質機(homogenizer)作為可進行這種處理的裝置,但並不限定於此。 A high-pressure homogenizer is preferably used as the apparatus capable of performing such treatment, but is not limited thereto.
在此作為衝撞用硬物的形狀係如:球狀、平板狀等,但並不限定於此。又,高壓噴射之噴嘴的直徑較佳為0.1~0.9mm,但並不限定於此。 Here, the shape of the impact hard object is, for example, a spherical shape or a flat shape, but is not limited thereto. Further, the diameter of the high pressure jet nozzle is preferably 0.1 to 0.9 mm, but is not limited thereto.
又,高壓噴射時,較佳係預先以粉碎機等將上述經砑光加工 之聚芳醯胺紙粉碎到其纖維長度的加權平均值為噴嘴直徑的3倍以下,較佳為2倍以下,更佳為1.5倍以下。若為1.5倍以下,則可有效抑制上述經砑光加工之聚芳醯胺紙堵塞噴嘴。 Further, in the case of high-pressure jetting, it is preferred to previously calender the above by a pulverizer or the like. The polyarsenamide paper is pulverized until the weight average of the fiber length is 3 times or less, preferably 2 times or less, more preferably 1.5 times or less. When it is 1.5 times or less, the above-mentioned calendered polyarsenamide paper clogging nozzle can be effectively suppressed.
粉碎上述經砑光加工之聚芳醯胺紙的方法較佳為使用乾式法、濕式法或兩種方法並行來粉碎而使其微粒子化的方法。乾式法係使用碎紙機(shredder)、軋碎機(crusher)、捏合機(kneader)等,在實際上不存在水分的情況下對聚芳醯胺紙進行衝撃而使其分解成微粒子的方法。又,濕式法係在水介質中對聚芳醯胺紙進行衝撃而使其粒度變小的方法。可有效實施這種濕式粉碎的設備係如高速分解機、精磨機(refiner)、打漿機(beater)等,但並不限定於此。 The method of pulverizing the above-mentioned calendered polyaramide paper is preferably a method of pulverizing and pulverizing it by a dry method, a wet method or both methods in parallel. The dry method uses a shredder, a crusher, a kneader, or the like to pulverize the polyamidamine paper into fine particles without actually having moisture. . Further, the wet method is a method in which polyarsenamide paper is washed in an aqueous medium to reduce the particle size. The apparatus capable of effectively performing such wet pulverization is, for example, a high-speed disintegrator, a refiner, a beater, or the like, but is not limited thereto.
在高壓噴射處理的條件方面,噴射壓力較佳係在70~300MPa的範圍內。噴射速度較佳係在300~900m/s的範圍內。 In terms of the conditions of the high pressure jet treatment, the injection pressure is preferably in the range of 70 to 300 MPa. The ejection speed is preferably in the range of 300 to 900 m/s.
又,當上述經砑光加工之聚芳醯胺紙浸漬於水中時,其濃度較佳為0.1~10wt%。浸漬於水中時,如有必要,可使用分散性提升劑、消泡劑等添加劑。 Further, when the above-mentioned calendered polyaramide paper is immersed in water, the concentration thereof is preferably from 0.1 to 10% by weight. When immersed in water, if necessary, additives such as a dispersibility enhancer and an antifoaming agent may be used.
如有必要,可重複進行多次高壓噴射處理,但次數過多則成本變高;更進一步言之,如將醯胺短纖維之部分切斷的作業持續進行,就不會停留在作為抄紙原料的短纖維形狀,故較為不佳。也就是說,上述經砑光加工之聚芳醯胺紙在經高壓噴射處理前後的纖維長度之加權平均值的保持率較佳為80%以上。 If necessary, the high-pressure jet treatment may be repeated a plurality of times, but if the number of times is too high, the cost becomes high; further, if the operation of cutting off the part of the short-cut fibers of the guanamine is continued, it does not stay as a raw material for papermaking. Short fiber shape, it is not good. That is, the retention ratio of the weighted average of the fiber lengths of the above-mentioned calendered polyaramide paper before and after the high pressure jet treatment is preferably 80% or more.
(體積平均粒度分布、粒徑峰值) (volume average particle size distribution, particle diameter peak)
在本發明中,體積平均粒度分布係為依體積基準所測得的粒 子分布。又,體積平均粒徑係為依體積基準所測得的粒徑。又,粒徑峰值係為體積平均粒度分布的峰值。另外,由於本發明之抄紙用原料具有纖維形狀、粒子形狀或不定形狀等的立體形狀,故係用粒徑峰值來定出抄紙用原料的大小、形狀。 In the present invention, the volume average particle size distribution is a particle measured on a volume basis. Sub-distribution. Further, the volume average particle diameter is a particle diameter measured on a volume basis. Further, the particle diameter peak is the peak of the volume average particle size distribution. In addition, since the raw material for papermaking of the present invention has a three-dimensional shape such as a fiber shape, a particle shape, or an indefinite shape, the size and shape of the raw material for papermaking are determined by the particle diameter peak.
又,吾人認為,在體積平均粒度分布中,位於10μm以上、未達100μm範圍內的粒徑峰值主要係表示分解後之聚芳醯胺短纖維的相對量;於高壓噴射處理後出現上述粒徑峰值,則表示出現聚芳醯胺短纖維。 Further, it is considered that, in the volume average particle size distribution, the peak of the particle diameter in the range of 10 μm or more and less than 100 μm mainly represents the relative amount of the polyarsenide short fibers after decomposition; the above particle diameter occurs after the high pressure jet treatment The peak value indicates the presence of polyarmine short fibers.
因此,本發明較佳係採用使在高壓噴射處理後之聚芳醯胺紙的體積平均粒度分布在10μm以上、未達100μm範圍內出現粒徑峰值的方式來進行高壓噴射處理,如此易使短纖維糾結,而提升耐熱性電絕緣片材的強度。 Therefore, the present invention preferably employs a high-pressure jet treatment in such a manner that a volume average particle size distribution of the polyamidamide paper after the high-pressure jet treatment is 10 μm or more and a particle diameter peak within a range of less than 100 μm, so that it is easy to be short. The fibers are entangled to enhance the strength of the heat-resistant electrically insulating sheet.
更佳者,係以下述方式進行高壓噴射處理:在高壓噴射處理前先粉碎聚芳醯胺紙,使高壓噴射處理前之聚芳醯胺紙的體積平均粒度分布中的粒徑峰值分別位於10μm以上、未達100μm的範圍內與100μm以上、未達1000μm的範圍內,並使在高壓噴射處理後,位於10μm以上、未達100μm的範圍內之粒徑峰值頻率增加、而位於100μm以上、未達1000μm以下的範圍內之粒徑峰值頻率減少。 More preferably, the high-pressure jet treatment is carried out in the following manner: the polyarylamide paper is pulverized before the high-pressure jet treatment, so that the particle diameter peaks in the volume average particle size distribution of the polyarylamide paper before the high-pressure jet treatment are respectively at 10 μm. In the range of less than 100 μm and in the range of 100 μm or more and less than 1000 μm, the peak frequency of the particle diameter in the range of 10 μm or more and less than 100 μm after the high-pressure jet treatment is increased, and is located at 100 μm or more. The peak frequency of the particle diameter in the range of up to 1000 μm is reduced.
吾人認為,在上述經砑光加工之聚芳醯胺紙的體積平均粒度分布中,位於10μm以上、未達100μm範圍內之粒徑峰值主要係表示分解後之聚芳醯胺短纖維的相對量,而位於100μm以上、未達1000μm範圍內之粒徑峰值主要係表示未分解之聚芳醯胺短纖維與聚芳醯胺纖條體之混合物的相對量;於高壓噴射處理後,前者的粒徑峰值頻率會增加,後者的粒徑峰 值頻率會減少,這表示聚芳醯胺短纖維的量相對增加,而未分解之聚芳醯胺短纖維與聚芳醯胺纖條體之混合物的量相對減少。 In our opinion, in the volume average particle size distribution of the above-mentioned calendered polyarylamide paper, the peak of the particle diameter in the range of 10 μm or more and less than 100 μm mainly indicates the relative amount of the polyarylamine short fibers after decomposition. The peak of the particle diameter in the range of 100 μm or more and less than 1000 μm mainly represents the relative amount of the mixture of the undecomposed polylinamide short fibers and the polyarylamine fibrids; after the high pressure jet treatment, the former particles The peak frequency of the diameter will increase, and the particle size peak of the latter The frequency of the values is reduced, which means that the amount of polyarmine short fibers is relatively increased, while the amount of the mixture of undecomposed polylinamide short fibers and polyarylamine fibrids is relatively reduced.
藉此,短纖維容易糾結,這不僅會提升耐熱性電絕緣片材的強度,亦可減少耐熱性電絕緣片材的厚度差問題。 Thereby, the short fibers are easily entangled, which not only improves the strength of the heat-resistant electrically insulating sheet, but also reduces the problem of the difference in thickness of the heat-resistant electrically insulating sheet.
(耐熱性電絕緣片材) (heat-resistant electrical insulation sheet)
本發明之耐熱性電絕緣片材係指含有該抄紙用原料的片狀物,一般而言,其厚度係在20μm~5mm的範圍內。更進一步言之,耐熱性電絕緣片材的基重一般為在10g/m2~5000g/m2的範圍內,較佳為在10g/m2~200g/m2的範圍內。 The heat-resistant electrically insulating sheet of the present invention is a sheet-like material containing the raw material for papermaking, and generally has a thickness in the range of 20 μm to 5 mm. Furthermore, the basis weight of the heat-resistant electrically insulating sheet is generally in the range of 10 g/m 2 to 5000 g/m 2 , preferably in the range of 10 g/m 2 to 200 g/m 2 .
在耐熱性電絕緣片材中,只要可達到預期的電絕緣性,對該抄紙用原料的含量並無特別限制,而在耐熱性電絕緣片材的製造中,為了保持製程強度,其含量較佳為5~80質量%;更進一步來說,為了得到充分的電絕緣性,其含量較佳為15~80質量%;更進一步來說,為了得到充分的強度,其含量更佳為30~80質量%。剩餘部分可為新的聚芳醯胺纖條體、或與聚芳醯胺短纖維的混合,但並不限定於此。 In the heat-resistant electrically insulating sheet, the content of the raw material for papermaking is not particularly limited as long as the desired electrical insulation can be achieved, and in the manufacture of the heat-resistant electrically insulating sheet, in order to maintain the process strength, the content is higher. Preferably, the content is 5 to 80% by mass; further, in order to obtain sufficient electrical insulation, the content is preferably 15 to 80% by mass; further, in order to obtain sufficient strength, the content is preferably 30~ 80% by mass. The remainder may be a new polyarylamine fibrid or a mixture with polyarylamine short fibers, but is not limited thereto.
耐熱性電絕緣片材一般係採用將上述的抄紙用原料與聚芳醯胺纖條體等混合後再將其薄片化的方法來製造。 The heat-resistant electrically insulating sheet is generally produced by a method in which the above-mentioned raw material for papermaking is mixed with a polyamidoamine fibrid or the like and then flaky.
製造片材時,可使用如將該抄紙用原料與聚芳醯胺纖條體進行乾式混合後,利用氣流形成薄片的方法;將上述抄紙用原料及聚芳醯胺纖條體在液體介質中分散混合後,投至具有液體通透性的支持體(例如網或帶),上而將其薄片化,再去除液體以將其乾燥的方法等;在前述方法中,較佳係選擇以水作為介質的所謂濕式製造法。 When the sheet is produced, a method of forming a sheet by air flow after dry-mixing the raw material for papermaking with a polyamidoamine fibrid, and using the raw material for papermaking and the polyarylamine fibrid in a liquid medium can be used. After dispersing and mixing, it is fed to a support having a liquid permeability (for example, a mesh or a belt), which is flaky, and then the liquid is removed to dry it. In the above method, it is preferred to select water. A so-called wet manufacturing method as a medium.
在濕式製造法中,一般係將至少含有該抄紙用原料、聚芳醯胺纖條體之單一種類或其混合物的水性漿液供給至抄紙機以使其分散之後,進行脫水、擠水及乾燥步驟,以得出片材而將其捲繞起來。抄紙機可利用長網抄紙機、圓網抄紙機、傾斜型抄紙機及將該等裝置組合得出的混合抄紙機等。在以混合抄紙機進行製造的情況下,可使摻合比例不同的漿液形成薄片並合為一體,而得到由複數紙層所形成之複合薄片。在進行抄紙時,如有必要,可使用分散性提升劑、消泡劑、紙力增強劑等的添加劑。 In the wet manufacturing method, an aqueous slurry containing at least the raw material for papermaking, a single type of polyarylene fibril, or a mixture thereof is supplied to a paper machine to be dispersed, and then dehydrated, squeezed, and dried. The step is to wind up the sheet to obtain the sheet. The paper machine can use a long net paper machine, a rotary paper machine, a tilt type paper machine, and a hybrid paper machine obtained by combining the same. In the case of production by a hybrid paper machine, the slurry having different blending ratios can be formed into a sheet and integrated to obtain a composite sheet formed of a plurality of paper layers. When performing papermaking, an additive such as a dispersibility improving agent, an antifoaming agent, or a paper strength enhancer may be used if necessary.
又,除此之外可添加其他纖維狀成分(例如聚芳醯胺纖維、聚苯硫醚(polyphenylene sulfide)纖維、聚醚醚酮(polyetheretherketone)纖維、纖維素系纖維、PVA系纖維、聚酯纖維、芳基化物(arylate)纖維、液晶聚酯纖維、聚萘二甲酸乙二酯(polyethylene naphthalate)纖維等的有機纖維;玻璃纖維、岩棉(rock wool)、石棉、硼纖維等的無機纖維玻璃纖維)。 Further, other fibrous components (for example, polyarylene fiber, polyphenylene sulfide fiber, polyetheretherketone fiber, cellulose fiber, PVA fiber, polyester may be added). Organic fibers such as fibers, arylate fibers, liquid crystal polyester fibers, polyethylene naphthalate fibers, inorganic fibers such as glass fibers, rock wool, asbestos, and boron fibers glass fiber).
在本發明之耐熱性電絕緣片材中,由於聚芳醯胺纖條體是一種具有優異特性的黏著劑,故可有效地補足微粒子及其他添加成分;而在本發明之耐熱性電絕緣片材製造中,不但可使原料的產率變好,同時亦可在片材內重疊成層狀,並使貫通孔減少,從而提升了電絕緣性。 In the heat-resistant electrically insulating sheet of the present invention, since the polyarylamine fibrid is an adhesive having excellent characteristics, it can effectively complement the fine particles and other additive components; and the heat-resistant electrical insulating sheet of the present invention In the material manufacturing, not only the yield of the raw material can be improved, but also the lamination can be layered in the sheet, and the through hole can be reduced, thereby improving the electrical insulation.
以此方式所得到的耐熱性電絕緣片材係在一對平板間或金屬製滾筒間以高溫高壓進行熱壓,藉此可提高密度、機械強度。在使用金屬製滾筒的情況下,例示的熱壓的條件雖為溫度在100~350℃、線壓在50~400kg/cm的範圍內,但並不限定於此。可不進行加熱操作,而僅以常溫加壓。熱壓時可堆疊複數耐熱性電絕緣片材。上述熱壓加工亦可以任意順序進行多次。 The heat-resistant electrically insulating sheet obtained in this manner is hot-pressed at a high temperature and a high pressure between a pair of flat plates or a metal drum, whereby density and mechanical strength can be improved. In the case of using a metal drum, the conditions of the hot pressing are exemplified by a temperature of 100 to 350 ° C and a linear pressure of 50 to 400 kg/cm, but the invention is not limited thereto. The heating operation may be omitted, and only the normal temperature is applied. A plurality of heat-resistant electrically insulating sheets may be stacked during hot pressing. The above hot press processing can also be performed multiple times in any order.
以下係以實施例來說明本發明。又,這些實施例係用於舉例說明本發明的內容,而未對本發明的內容造成任何限制。 The invention is illustrated by the following examples. Further, these examples are for illustrating the contents of the present invention without any limitation on the contents of the present invention.
實施例 Example
(測量方法) (Measurement methods)
(1)粒度分布之測量 (1) Measurement of particle size distribution
藉由光散射式的粒度分布測量儀(堀場製作所製,雷射繞射/散射式粒度分布裝置LA-910)來測量粒度分布。 The particle size distribution was measured by a light scattering type particle size distribution measuring instrument (manufactured by Horiba, Ltd., laser diffraction/scattering type particle size distribution device LA-910).
(2)纖維長度之加權平均值 (2) Weighted average of fiber length
使用Op Test Equipment公司製的纖維質量分析儀(Fiber Quality Analyzer),就約4000個微粒子來測量其纖維長度的加權平均值。 A weighted average of the fiber lengths was measured with about 4,000 particles using a Fiber Quality Analyzer manufactured by Op Test Equipment.
(3)基重、厚度之測量 (3) Measurement of basis weight and thickness
依據JIS C2300-2進行。 According to JIS C2300-2.
關於厚度差,係測量連續40點的厚度,以其標準差作為厚度差。 Regarding the difference in thickness, the thickness of 40 consecutive points was measured, and the standard deviation was used as the thickness difference.
(4)密度之計算 (4) Calculation of density
以基重÷厚度計算。 Calculated by basis weight ÷ thickness.
(5)拉伸強度之測量 (5) Measurement of tensile strength
在寬度15mm、夾頭間隔50mm、拉伸速度50mm/分的條件下操作TENSILON拉伸試驗機進行測量。 The TENSILON tensile tester was operated under the conditions of a width of 15 mm, a collet interval of 50 mm, and a tensile speed of 50 mm/min.
(6)透氣度 (6) Air permeability
使用JIS P8117規定之GURLEY式透氣度測試裝置,測量100cc(0.1dm3)的空氣透過一樣品片材(面積642mm2)的時間(秒),其中該樣品片材上壓有一具有外徑為28.6mm之圓孔的壓板。 The time (seconds) at which 100 cc (0.1 dm 3 ) of air was transmitted through a sample sheet (area 642 mm 2 ) was measured using a GURLEY type gas permeability test apparatus prescribed in JIS P8117, wherein the sample sheet was pressed with an outer diameter of 28.6. The platen of the round hole of mm.
(原料製備1) (Material preparation 1)
使用日本特開昭52-15621號公報中以定子(stator)與轉子之組合所構成的紙漿粒子之製造裝置(濕式沉澱裝置),來製造聚間伸苯基間苯二甲醯胺之纖條體。以分解設備、打漿設備進行處理,將纖維長度的加權平均值調節為0.9mm(聚芳醯胺纖條體之游離度:100ml(加拿大遊離度))_。 A fiber-making device for producing pulp particles (wet-precipitation device) comprising a combination of a stator and a rotor in the Japanese Patent Laid-Open Publication No. Sho 52-15621 is used to produce a fiber of poly(phenylphenylisophthalamide). Strip. The treatment was carried out by a decomposition apparatus and a beating apparatus, and the weighted average value of the fiber length was adjusted to 0.9 mm (the freeness of the polyarylamine fibrids: 100 ml (Canadian freeness)).
另一方面,將杜拜公司製的間位聚芳醯胺(metaaramid)纖維(NOMEX(註冊商標),單線纖度2丹尼)切成長度6mm(下稱「醯胺短纖維」)。 On the other hand, a meta-aramid fiber (NOMEX (registered trademark), single-strand denier 2 Danny) manufactured by Dubai Company was cut into a length of 6 mm (hereinafter referred to as "melamine short fiber").
(經砑光加工之聚芳醯胺紙的製造) (Manufacture of polyarsenide paper by calendering)
分別使所製備的聚芳醯胺纖條體與聚芳醯胺短纖維在水中分散而製成漿液。以使纖條體與聚芳醯胺短纖維的摻合比例(重量比)為1/1的方式混合,並以TAPPI式手工抄紙設備(剖面面積為625cm2)製成片狀物。接著,以金屬製砑光輥(calender roll)在溫度330℃、線壓300kg/cm的條件下對前述片狀物進行熱壓加工,而得到經砑光加工之聚芳醯胺紙。 The prepared polyarylamine fibrids and polyarylamine short fibers were separately dispersed in water to prepare a slurry. The blending ratio (weight ratio) of the fibrids and the polyamidamine short fibers was 1/1, and a sheet was formed by a TAPPI-type hand-made papermaking apparatus (cross-sectional area: 625 cm 2 ). Next, the sheet-like material was subjected to hot press processing at a temperature of 330 ° C and a linear pressure of 300 kg/cm by a metal calender roll to obtain a calendered polyaramide paper.
(原料製備2) (Material Preparation 2)
以下述方法準備材料:將上述經砑光加工之聚芳醯胺紙以碎紙機進行粉碎,並使其透過孔徑為1mm的篩(以下稱為Φ1聚芳醯胺紙)(纖維長度的加權平均值約為噴嘴直徑的80%)。 The material was prepared in the following manner: the above-mentioned calendered polyaramide paper was pulverized by a paper shredder and passed through a sieve having a pore size of 1 mm (hereinafter referred to as Φ1 polyamidamine paper) (weighting of fiber length) The average value is approximately 80% of the nozzle diameter).
以上述Φ1聚芳醯胺紙8質量分、水92質量分的比例混合,並以高壓均質機(杉野機械(Sugino Machine)公司製STAR BURST100 HJP-25080:噴嘴直徑0.5mm)在表1所示之條件下進行高壓噴射處理,並使其撞 擊衝撞用硬物(陶瓷)而碎裂,形成抄紙用原料。 The mixture was mixed with the above-mentioned Φ1 polyamidamine paper in an amount of 8 parts by mass and water in an amount of 92 parts by mass, and was shown in Table 1 by a high-pressure homogenizer (STAR BURST100 HJP-25080 manufactured by Sugino Machine Co., Ltd.: nozzle diameter: 0.5 mm). Under high pressure jet treatment, and make it hit The impact is broken by a hard object (ceramic) to form a raw material for papermaking.
(實施例1~3、對照例) (Examples 1 to 3, Comparative Examples)
(耐熱性電絕緣片材之製造) (Manufacture of heat-resistant electrical insulating sheet)
分別將所製備的Φ1聚芳醯胺紙、所製備的抄紙用原料、所製備的聚芳醯胺纖條體分散於水中以製成漿液。以表1所示之摻合比例(質量比)混合前述漿液,並以TAPPI手工抄紙機(剖面面積為625cm2)製成片狀物。接著,以金屬製砑光輥在溫度330℃、線壓300kg/cm的條件下對前述片狀物進行熱壓加工,而得到耐熱性電絕緣片材。以此方式所得之耐熱性電絕緣片材的主要特性數值係如表1所示。 The prepared Φ1 polyarsenamide paper, the prepared raw material for papermaking, and the prepared polyamidamine fibrids were respectively dispersed in water to prepare a slurry. The slurry was mixed at a blending ratio (mass ratio) shown in Table 1, and formed into a sheet by a TAPPI hand-held paper machine (sectional area: 625 cm 2 ). Then, the sheet-like object was subjected to hot press processing under the conditions of a temperature of 330 ° C and a linear pressure of 300 kg/cm by a metal calender roll to obtain a heat-resistant electrically insulating sheet. The main characteristic values of the heat-resistant electrically insulating sheet obtained in this manner are shown in Table 1.
從表1的結果可知,與高壓噴射處理前(對照例)相較之下,本發明(實施例1~3)之耐熱性電絕緣片材依然保持其纖維長度的加權平均值,且聚芳醯胺短纖維成分亦幾乎沒有被進一步切斷,故其強度高、厚度差小、更進一步在250℃處理10分鐘後亦未發現外觀變化,故可作為耐熱性電絕緣片材。又,吾人認為,增加相當於長度為0.3~0.4mm之聚芳醯胺短纖維的成分(相當於粒徑峰值1)後,會使透氣度變低,且在表面產生細微凹凸,而與其他的片材、樹脂等貼合時的黏合面積變廣,故特別可作為與絕 緣膜、絕緣樹脂貼合之層壓板所用的耐熱性電絕緣片材。 From the results of Table 1, it is understood that the heat-resistant electrically insulating sheets of the present invention (Examples 1 to 3) maintain a weighted average of the fiber lengths before the high-pressure jet treatment (Comparative Example), and Ju Fang Since the melamine short fiber component was hardly cut off, the strength was high and the thickness difference was small. Further, no change in appearance was observed even after the treatment at 250 ° C for 10 minutes, so that it could be used as a heat-resistant electrical insulating sheet. Moreover, it is considered that the addition of a component (corresponding to a particle diameter peak 1) of a polyarsenamide short fiber having a length of 0.3 to 0.4 mm causes a decrease in air permeability and generation of fine unevenness on the surface, and other When the sheet, the resin, and the like are bonded, the bonding area is widened, so that it is particularly useful as a A heat-resistant electrically insulating sheet used for a laminate of a film and an insulating resin.
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CN104846447B (en) * | 2015-04-15 | 2017-04-12 | 南通大学 | Fibrid continuous production equipment |
CN106758484B (en) * | 2015-11-24 | 2019-08-09 | 株洲时代新材料科技股份有限公司 | A kind of preparation method of aramid fiber cardboard |
KR101975318B1 (en) * | 2017-06-21 | 2019-08-28 | 한국섬유개발연구원 | Apparatus for Forming Wet Non-Woven Fabric |
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05272091A (en) * | 1992-03-18 | 1993-10-19 | New Oji Paper Co Ltd | Production of heat-insulating paper |
JPH07243189A (en) * | 1994-03-01 | 1995-09-19 | Teijin Ltd | Production of porous formed material of aramid |
JP2004047914A (en) * | 2001-07-25 | 2004-02-12 | Mitsubishi Paper Mills Ltd | Separator for capacitor |
CN100374210C (en) * | 2006-04-24 | 2008-03-12 | 南昌大学 | fluid impingement cavity |
CN100425349C (en) * | 2006-04-24 | 2008-10-15 | 南昌大学 | Striking cavity for liquid-phase super-fine disintegration |
JP2009277653A (en) * | 2008-04-18 | 2009-11-26 | Toray Ind Inc | Electrical insulating paper |
JP2012135703A (en) * | 2010-12-24 | 2012-07-19 | Tokuyama Corp | Method for recovering high purity gypsum powder from gypsum board wasted material at high yield |
TW201237891A (en) * | 2011-03-02 | 2012-09-16 | Dupont Teijin Advanced Papers Ltd | Heat-resistant electrically insulating sheet material and method for producing same |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5026456A (en) | 1990-06-14 | 1991-06-25 | E. I. Du Pont De Nemours And Company | Aramid papers containing aramid paper pulp |
JPH0860588A (en) * | 1994-08-24 | 1996-03-05 | Teijin Ltd | Production of high-modulus paper |
JPH1054000A (en) * | 1996-08-05 | 1998-02-24 | Nippon Aramido Kk | Para-oriented aromatic polyamide paper and its production |
JP3206500B2 (en) * | 1997-07-02 | 2001-09-10 | 王子製紙株式会社 | Processing method of raw materials for laminated substrate |
US5998309A (en) * | 1997-07-17 | 1999-12-07 | E. I. Du Pont De Nemours And Company | Molded aramid sheets |
EP0994215B1 (en) * | 1998-10-15 | 2003-06-04 | Teijin Limited | Wholly aromatic polyamide fiber synthetic paper sheet |
JP2003290676A (en) | 2002-03-29 | 2003-10-14 | Mitsubishi Paper Mills Ltd | Method for crushing laminated board, method for recycling crushed material, and heat-resistant electrical insulating paper |
ATE449210T1 (en) * | 2006-09-12 | 2009-12-15 | Meadwestvaco Corp | CARDBOARD WITH MICROPLATE-SHAPED CELLULOSE PARTICLES |
JP5665690B2 (en) * | 2011-08-18 | 2015-02-04 | デュポン帝人アドバンスドペーパー株式会社 | Papermaking raw material manufacturing method, obtained papermaking raw material, and heat-resistant electrical insulating sheet material using the raw material |
-
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Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05272091A (en) * | 1992-03-18 | 1993-10-19 | New Oji Paper Co Ltd | Production of heat-insulating paper |
JPH07243189A (en) * | 1994-03-01 | 1995-09-19 | Teijin Ltd | Production of porous formed material of aramid |
JP2004047914A (en) * | 2001-07-25 | 2004-02-12 | Mitsubishi Paper Mills Ltd | Separator for capacitor |
CN100374210C (en) * | 2006-04-24 | 2008-03-12 | 南昌大学 | fluid impingement cavity |
CN100425349C (en) * | 2006-04-24 | 2008-10-15 | 南昌大学 | Striking cavity for liquid-phase super-fine disintegration |
JP2009277653A (en) * | 2008-04-18 | 2009-11-26 | Toray Ind Inc | Electrical insulating paper |
JP2012135703A (en) * | 2010-12-24 | 2012-07-19 | Tokuyama Corp | Method for recovering high purity gypsum powder from gypsum board wasted material at high yield |
TW201237891A (en) * | 2011-03-02 | 2012-09-16 | Dupont Teijin Advanced Papers Ltd | Heat-resistant electrically insulating sheet material and method for producing same |
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