JPH01286850A - Continuous manufacture of laminate - Google Patents
Continuous manufacture of laminateInfo
- Publication number
- JPH01286850A JPH01286850A JP63116515A JP11651588A JPH01286850A JP H01286850 A JPH01286850 A JP H01286850A JP 63116515 A JP63116515 A JP 63116515A JP 11651588 A JP11651588 A JP 11651588A JP H01286850 A JPH01286850 A JP H01286850A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- solution
- impregnating
- base materials
- side chain
- 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.)
- Pending
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 229920005989 resin Polymers 0.000 claims abstract description 53
- 239000011347 resin Substances 0.000 claims abstract description 53
- 239000000463 material Substances 0.000 claims abstract description 32
- 238000000034 method Methods 0.000 claims abstract description 14
- 239000011342 resin composition Substances 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 25
- 238000011437 continuous method Methods 0.000 claims description 2
- 239000000178 monomer Substances 0.000 abstract description 27
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 abstract description 15
- 229920002554 vinyl polymer Polymers 0.000 abstract description 15
- 238000004132 cross linking Methods 0.000 abstract description 7
- 238000010438 heat treatment Methods 0.000 abstract description 7
- 238000005470 impregnation Methods 0.000 abstract description 5
- 238000007791 dehumidification Methods 0.000 abstract description 3
- 239000004640 Melamine resin Substances 0.000 abstract description 2
- 229920000877 Melamine resin Polymers 0.000 abstract description 2
- 125000000524 functional group Chemical group 0.000 description 17
- -1 ethylene, propylene, butadiene Chemical class 0.000 description 9
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 8
- 239000000123 paper Substances 0.000 description 7
- 239000002184 metal Substances 0.000 description 5
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 125000003700 epoxy group Chemical group 0.000 description 4
- 150000002430 hydrocarbons Chemical group 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 2
- SBYMUDUGTIKLCR-UHFFFAOYSA-N 2-chloroethenylbenzene Chemical compound ClC=CC1=CC=CC=C1 SBYMUDUGTIKLCR-UHFFFAOYSA-N 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 2
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 2
- UIWXSTHGICQLQT-UHFFFAOYSA-N ethenyl propanoate Chemical compound CCC(=O)OC=C UIWXSTHGICQLQT-UHFFFAOYSA-N 0.000 description 2
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 2
- 239000003063 flame retardant Substances 0.000 description 2
- 239000011888 foil Substances 0.000 description 2
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000005011 phenolic resin Substances 0.000 description 2
- 229920001568 phenolic resin Polymers 0.000 description 2
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical compound C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 2
- 229920006337 unsaturated polyester resin Polymers 0.000 description 2
- JHPBZFOKBAGZBL-UHFFFAOYSA-N (3-hydroxy-2,2,4-trimethylpentyl) 2-methylprop-2-enoate Chemical compound CC(C)C(O)C(C)(C)COC(=O)C(C)=C JHPBZFOKBAGZBL-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 1
- GOXQRTZXKQZDDN-UHFFFAOYSA-N 2-Ethylhexyl acrylate Chemical compound CCCCC(CC)COC(=O)C=C GOXQRTZXKQZDDN-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- OMIGHNLMNHATMP-UHFFFAOYSA-N 2-hydroxyethyl prop-2-enoate Chemical compound OCCOC(=O)C=C OMIGHNLMNHATMP-UHFFFAOYSA-N 0.000 description 1
- VHSHLMUCYSAUQU-UHFFFAOYSA-N 2-hydroxypropyl methacrylate Chemical compound CC(O)COC(=O)C(C)=C VHSHLMUCYSAUQU-UHFFFAOYSA-N 0.000 description 1
- GWZMWHWAWHPNHN-UHFFFAOYSA-N 2-hydroxypropyl prop-2-enoate Chemical compound CC(O)COC(=O)C=C GWZMWHWAWHPNHN-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- LCFVJGUPQDGYKZ-UHFFFAOYSA-N Bisphenol A diglycidyl ether Chemical compound C=1C=C(OCC2OC2)C=CC=1C(C)(C)C(C=C1)=CC=C1OCC1CO1 LCFVJGUPQDGYKZ-UHFFFAOYSA-N 0.000 description 1
- GAWIXWVDTYZWAW-UHFFFAOYSA-N C[CH]O Chemical group C[CH]O GAWIXWVDTYZWAW-UHFFFAOYSA-N 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- CNCOEDDPFOAUMB-UHFFFAOYSA-N N-Methylolacrylamide Chemical compound OCNC(=O)C=C CNCOEDDPFOAUMB-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 125000003647 acryloyl group Chemical group O=C([*])C([H])=C([H])[H] 0.000 description 1
- 125000002723 alicyclic group Chemical group 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- 125000002029 aromatic hydrocarbon group Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- AOJOEFVRHOZDFN-UHFFFAOYSA-N benzyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC1=CC=CC=C1 AOJOEFVRHOZDFN-UHFFFAOYSA-N 0.000 description 1
- INLLPKCGLOXCIV-UHFFFAOYSA-N bromoethene Chemical compound BrC=C INLLPKCGLOXCIV-UHFFFAOYSA-N 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 150000001721 carbon Chemical group 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JBSLOWBPDRZSMB-FPLPWBNLSA-N dibutyl (z)-but-2-enedioate Chemical compound CCCCOC(=O)\C=C/C(=O)OCCCC JBSLOWBPDRZSMB-FPLPWBNLSA-N 0.000 description 1
- TVWTZAGVNBPXHU-FOCLMDBBSA-N dioctyl (e)-but-2-enedioate Chemical compound CCCCCCCCOC(=O)\C=C\C(=O)OCCCCCCCC TVWTZAGVNBPXHU-FOCLMDBBSA-N 0.000 description 1
- GMSCBRSQMRDRCD-UHFFFAOYSA-N dodecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCOC(=O)C(C)=C GMSCBRSQMRDRCD-UHFFFAOYSA-N 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- ABUWPPJBRQFDGF-UHFFFAOYSA-N ethyl n,n-bis(ethenyl)carbamate Chemical class CCOC(=O)N(C=C)C=C ABUWPPJBRQFDGF-UHFFFAOYSA-N 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 239000012796 inorganic flame retardant Substances 0.000 description 1
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000005267 main chain polymer Substances 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- RPQRDASANLAFCM-UHFFFAOYSA-N oxiran-2-ylmethyl prop-2-enoate Chemical compound C=CC(=O)OCC1CO1 RPQRDASANLAFCM-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000007348 radical reaction Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- B32B38/00—Ancillary operations in connection with laminating processes
-
- 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
- H05K3/00—Apparatus or processes for manufacturing printed circuits
- H05K3/02—Apparatus or processes for manufacturing printed circuits in which the conductive material is applied to the surface of the insulating support and is thereafter removed from such areas of the surface which are not intended for current conducting or shielding
- H05K3/022—Processes for manufacturing precursors of printed circuits, i.e. copper-clad substrates
Landscapes
- Laminated Bodies (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
本発明は積層板の連続的製造方法に関し、更に詳しくは
、樹脂液を含浸させつつ積層板を連続的に製造する方法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for continuously manufacturing a laminate, and more particularly to a method for continuously manufacturing a laminate while impregnating it with a resin liquid.
[従来の技術]
従来、フェノール樹脂を用いる例もあるが、反応副生物
による積層板の部分的浮き上り等を防止するため50k
g/cd以上の成型圧が必要であり、連続的製造法にお
いて上記のような圧力を連続的に確保することは極めて
困難である。[Prior art] Conventionally, phenolic resin has been used in some cases, but in order to prevent partial lifting of the laminate due to reaction by-products, 50k resin was used.
A molding pressure of more than g/cd is required, and it is extremely difficult to continuously secure the above pressure in a continuous manufacturing method.
熱硬化性樹脂で硬化の際に縮合水やガス等の反応副生成
分を実質的に発生しない樹脂を用いれば、加圧圧力を低
下させることはできる。このような樹脂としては不飽和
ポリエステル樹脂があり、そのスチレン溶液の場合はエ
ンドレスベルトで積層体の上下面から軽く押える程度で
良い。逆に高い圧力のもとでは、その低粘性にもとづき
基材間に存在する樹脂液はもちろん基材内に含まれる樹
脂液までも排出してしまい積層体としての性能を損う欠
点がある。By using a thermosetting resin that does not substantially generate reaction byproducts such as condensed water and gas during curing, the pressurizing pressure can be reduced. Such resins include unsaturated polyester resins, and in the case of a styrene solution thereof, it is sufficient to lightly press the laminate from the top and bottom surfaces with an endless belt. Conversely, under high pressure, due to its low viscosity, not only the resin liquid existing between the base materials but also the resin liquid contained within the base materials is discharged, impairing the performance of the laminate.
しかし圧力が低い場合は、基材間に樹脂液のみの硬化層
ができ、積層板の強度、剛性の両面において望ましくな
い。この観点より、加圧して基材同士を接触させること
は望ましい。However, if the pressure is low, a cured layer consisting only of resin liquid is formed between the base materials, which is undesirable in terms of both the strength and rigidity of the laminate. From this point of view, it is desirable to bring the base materials into contact with each other by applying pressure.
この基材間の接触をさせるには、基材内含有樹脂液の排
出を伴っては上記不飽和ポリエステルの場合と同じにな
ってしまうので加圧下にできるだけ基材表面にある含浸
樹脂液を基材内にある液よりも多く排除することができ
ることが望ましい。In order to make this contact between the base materials, the impregnated resin liquid on the surface of the base material should be used as much as possible under pressure, since if the resin liquid contained in the base material is discharged, the result will be the same as in the case of unsaturated polyester. It is desirable to be able to remove more liquid than is present in the material.
またこれに適する樹脂もまだ見つかっていない。Also, a resin suitable for this has not yet been found.
[発明が解決しようとする課題]
従って本発明の目的は含浸樹脂液のうち、可及的に基材
表面のものをより少なくして基材間の接触を図る方法を
見出すことにある。[Problems to be Solved by the Invention] Therefore, an object of the present invention is to find a method for reducing the amount of the impregnating resin liquid on the surface of the substrate as much as possible to achieve contact between the substrates.
[課題を解決するための手段]
本発明者はこの課題を解決するため鋭意研究をのを絞る
と基材内には含浸樹脂は存在しても、基材間には殆ど存
在しなくなることを見出し、本発明を完成した。即ち、
本発明の要旨は紙基材に側鎖二重結合型樹脂を主成分と
する樹脂組成物を連続的に含浸させた後その複数を重ね
あわせた状態で再度同一含浸樹脂液中に導き該液内の絞
りローラーを通してからひき出し、加圧下に余剰含浸樹
脂液を排出させつつ加熱硬化する積層板の連続的製造方
法にある。[Means for Solving the Problem] In order to solve this problem, the inventor of the present invention has found that even if the impregnating resin is present within the base material, it will hardly be present between the base materials if the inventors concentrate on their research. The present invention has been completed. That is,
The gist of the present invention is to continuously impregnate a paper base material with a resin composition containing a side chain double bond type resin as a main component, and then to superimpose a plurality of the resin compositions and then introduce the same impregnating resin solution again into the same impregnated resin solution. This is a continuous method for manufacturing a laminate, in which the material is passed through a squeezing roller inside, drawn out, and heated and cured while draining excess impregnated resin liquid under pressure.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明にいう側鎖二重結合型樹脂とは、主鎖と側鎖とか
らなる重合体であって、主鎖は官能基を有するビニルモ
ノマー単位を含む幹ポリマーであり、側鎖は該主鎖の官
能基を介して構成されてなるラジカル反応可能な炭素−
炭素二重結合を有する枝である側鎖二重結合型樹脂を指
し、側鎖二重結合型樹脂の主鎖を構成するビニルモノマ
ー単位とは官能基を有するとニルモノマー単位を必須単
位とし、これに必要に応じ官能基を持たないビニルモノ
マー単位を含ませたものであり、これらが重合して主鎖
が構成される。The side chain double bond type resin referred to in the present invention is a polymer consisting of a main chain and a side chain, where the main chain is a backbone polymer containing a vinyl monomer unit having a functional group, and the side chain is a backbone polymer containing a vinyl monomer unit having a functional group. A radically reactive carbon formed through the functional group of the chain.
Refers to a side chain double bond type resin which is a branch having a carbon double bond, and the vinyl monomer unit that constitutes the main chain of the side chain double bond type resin is an essential unit when it has a functional group. It contains vinyl monomer units that do not have functional groups as necessary, and these polymerize to form the main chain.
上記必須単位を構成するモノマーとしてはアクリル酸、
メタクリル酸、無水マレイン酸、マレイン酸モノエステ
ル等の官能基としてカルボキシル基を有するビニル単量
体、グリシジルメタクリレート、グリシジルアクリレー
ト等の官能基としてグリシジル基を有するビニル単量体
その他アリルアルコール、2−ヒドロキシエチルメタク
リレート、2−ヒドロキシエチルアクリレート、2−ヒ
ドロキシプロピルメタクリレート、2−ヒドロキシプロ
ピルアクリレート、N−メ千ロールアクリルアミド等の
官能基としてヒドロキシ基を有するビニル単量体等が代
表的であり、特にアクリル酸及びメタクリル酸が最も好
ましく用いられる。Monomers constituting the above essential units include acrylic acid,
Vinyl monomers having a carboxyl group as a functional group such as methacrylic acid, maleic anhydride, and maleic acid monoester, vinyl monomers having a glycidyl group as a functional group such as glycidyl methacrylate, glycidyl acrylate, etc. Allyl alcohol, 2-hydroxy Typical examples include vinyl monomers having a hydroxyl group as a functional group, such as ethyl methacrylate, 2-hydroxyethyl acrylate, 2-hydroxypropyl methacrylate, 2-hydroxypropyl acrylate, and N-methylol acrylamide. and methacrylic acid are most preferably used.
本発明における官能基を有するとニルモノマー単位とは
主鎖を重合により形成する場合に活性な官能基として存
在させる場合のほか、後述の側鎖を予め該モノマーの官
能基と反応させておいて重合させて主鎖を形成する場合
の区別なく側鎖を主鎖に形成せしめる役目をした官能基
がある形のビニルモノマー単位を指す。In the present invention, a functional group-containing monomer unit may be present as an active functional group when the main chain is formed by polymerization, or may be polymerized by reacting the side chain described below with the functional group of the monomer in advance. It refers to a type of vinyl monomer unit that has a functional group that serves to form a side chain into the main chain, regardless of whether the main chain is formed by forming a side chain.
官能基を有しないとニルモノマーとしては、スチレン、
α−メチルスチレン、クロロスチレン、ビニルトルエン
、塩化ビニル、塩化ビニリデン、臭化ビニル、アクリロ
ニトリル、エチレン、プロピレン、ブタジェン、アクリ
ル酸エステル、メタクリル酸エステル、酢酸ビニル、プ
ロピオン酸ビニル、マレイン酸ジエステル、エチルビニ
ルベンゼン等が挙げられる。Non-functional monomers include styrene,
α-methylstyrene, chlorostyrene, vinyltoluene, vinyl chloride, vinylidene chloride, vinyl bromide, acrylonitrile, ethylene, propylene, butadiene, acrylic ester, methacrylic ester, vinyl acetate, vinyl propionate, diester maleate, ethyl vinyl Examples include benzene.
これらビニルモノマー単位から構成される主鎖の重量平
均分子量は5000ないし400,000であり、好適
には10,000ないし200.000である。この値
は、側鎖の種類に対応させて適宜選択される。この分子
量は積層板としての物性とか、含浸性に影響し、500
0未満では硬化後の積層板の機械的物性が不十分となり
、逆に400,000を超えると基材(紙等)への樹脂
含浸性が劣り、いずれも好ましくない。The weight average molecular weight of the main chain composed of these vinyl monomer units is from 5,000 to 400,000, preferably from 10,000 to 200,000. This value is appropriately selected depending on the type of side chain. This molecular weight affects the physical properties of the laminate and impregnating properties, and
If it is less than 0, the mechanical properties of the cured laminate will be insufficient, and if it exceeds 400,000, the resin impregnation into the base material (paper etc.) will be poor, both of which are not preferred.
主鎖中の官能基を有するモノマー単位の量は側鎖の密度
に関係し、側鎖間の硬化反応性に影響するので適宜の比
率が選ばれるが、主鎖10001H中側鎖密度は0.1
〜2モルが好ましく、より好適には0.4〜1.5モル
である。The amount of monomer units having functional groups in the main chain is related to the density of the side chains, and since it affects the curing reactivity between the side chains, an appropriate ratio is selected, but the side chain density in the main chain 10001H is 0. 1
-2 mol is preferable, and 0.4-1.5 mol is more suitable.
本発明にいう側鎖とは、末端又は中間に>C−Cくなる
二重結合を有するもので、前記主鎖にその官能基を介し
て技を構成しているものを指すが代表的なものとしては
、
(以下余白)
工 =
0□Q
C+J 0
op−0(!10
u u
l CJ
+ 1
u=o l工 E
Ol O:
工U−0100−CJ
I Q=Ol
1等が一般式として例示できる。The side chain referred to in the present invention refers to a chain that has a >C-C double bond at the end or in the middle, and that forms a chain in the main chain via its functional group, but typical As a matter of fact, (blank space below)
l C.J.
+1
u=o l engineering E
Ol O:
Engineering U-0100-CJ I Q=Ol
1 etc. can be exemplified as a general formula.
(I)式中R1〜R3は水素又はメチル基であり、nは
0〜5の整数を示し、 (II)式中R4は水素又はメ
チル基であり、Ll及びL2は一〇−又は−NH−を示
し、Xl及びX2はC2ないし01Bの炭化水素基又は
エーテル結合により連結した炭化水素基を示し、かっこ
のX 及びX2において該X 及びX2とI目間る酸素
と結合している炭素原子は1級又は2級炭素であり、B
はC2oまでの脂肪族、脂環族又は芳香族炭化水素基で
ある。(I) In the formula, R1 to R3 are hydrogen or a methyl group, n represents an integer of 0 to 5, (II) In the formula, R4 is hydrogen or a methyl group, and Ll and L2 are 10- or -NH -, Xl and X2 represent a C2 to 01B hydrocarbon group or a hydrocarbon group connected by an ether bond, and in parentheses X and X2, the carbon atom bonded to the oxygen between X and X2 and I is a primary or secondary carbon, and B
is an aliphatic, alicyclic or aromatic hydrocarbon group up to C2o.
(III)式中R5は水素又はメチル基である。(III) In the formula, R5 is hydrogen or a methyl group.
なお、本発明に係る側鎖二重結合型樹脂の側鎖はこれら
に限られるものではなく、側鎖間に架橋ビニルモノマー
によりラジカル反応によって架橋を形成し得るものであ
れば適用しうる。Note that the side chains of the side chain double bond type resin according to the present invention are not limited to these, and any type of side chain that can form a crosslink between side chains by a radical reaction using a crosslinking vinyl monomer can be used.
本発明において上記主鎖を構成する重合体に対して側鎖
末端に二重結合を有する側鎖を導入する方法としては多
様な方法が採用され得る。幾つかの例を挙げれば次のよ
うである。In the present invention, various methods can be employed to introduce a side chain having a double bond at the end of the side chain into the polymer constituting the main chain. Some examples are as follows.
(1)主鎖の官能基のカルボキシル基に対してビスフェ
ノール型ジグリシジルエーテルタイブエボキシ基のよう
なジェポキシ基を有する化合物の一方のエポキシ基を反
応させ、残るエポキシ基と(メタ)アクリル酸を反応さ
せる。(1) One epoxy group of a compound having a jepoxy group such as bisphenol diglycidyl ether type epoxy group is reacted with the carboxyl group of the functional group of the main chain, and the remaining epoxy group is reacted with (meth)acrylic acid. let
(2)主鎖の官能基のカルボキシル基とグリシジル(メ
タ)アクリレートを反応させる。(2) React the carboxyl group of the main chain functional group with glycidyl (meth)acrylate.
(3)主鎖の官能基のエポキシ基と(メタ)アクリル酸
とを反応させる。(3) React the epoxy group of the main chain functional group with (meth)acrylic acid.
(4) ジイソシアネート化合物にヒドロキシエチル
(メタ)アクリレートを反応させ、モノイソシアネート
を主成分としジイソシアネート化合物を殆ど含まない反
応物を作っておき、この反応物に含まれるイソシアネー
ト基を主鎖ポリマーの水酸基と反応させる。(4) A diisocyanate compound is reacted with hydroxyethyl (meth)acrylate to prepare a reaction product containing monoisocyanate as the main component and almost no diisocyanate compound, and the isocyanate groups contained in this reaction product are combined with the hydroxyl groups of the main chain polymer. Make it react.
例示した方法では主鎖の共重合を先に行ったが、当然な
がら本発明においては、予め側鎖を構成する反応を先に
行い、かかるモノマーを最後に共重合させて側鎖末端に
(メタ)アクリロイル基を含む側鎖二重結合型樹脂を製
造してもよい。In the exemplified method, the main chain was copolymerized first, but in the present invention, of course, the reaction to form the side chain is carried out first, and such monomers are finally copolymerized to form the side chain terminal (method). ) A side chain double bond type resin containing an acryloyl group may be produced.
本発明における側鎖二重結合型樹脂はスチレン等の架橋
用とニルモノマーで希釈され、重合開始剤が加えられて
用いられる。更に公知のハロゲン系難燃剤及び/又は無
機系難燃剤を必要に応じて添加することにより難燃化さ
れた組成物としても用いられる。The side chain double bond type resin in the present invention is diluted with a crosslinking monomer such as styrene, and a polymerization initiator is added before use. Furthermore, it can also be used as a flame-retardant composition by adding a known halogen flame retardant and/or inorganic flame retardant as necessary.
なお、前記架橋用ビニルモノマーとしては特に限定され
ないが、該モノマーのうち単官能性炭化水素系単量体に
は、スチレン、ビニルトルエン、クロロスチレン、アク
リル酸メチル、アクリル酸エチル、アクリル酸ブチル、
アクリル酸−2−エチルヘキシル、メタクリル酸メチル
、メタクリル酸エチル、メタクリル酸ブチル、メタクリ
ル酸ラウリル、メタクリル酸ベンジル、マレイン酸ジブ
チル、マレイン酸ジオクチル、酢酸ビニル、プロピオン
酸ビニル等が包含される。これらのモノマーは2種以上
を混合して用いてもよい。The crosslinking vinyl monomer is not particularly limited, but among the monomers, monofunctional hydrocarbon monomers include styrene, vinyltoluene, chlorostyrene, methyl acrylate, ethyl acrylate, butyl acrylate,
Included are 2-ethylhexyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate, lauryl methacrylate, benzyl methacrylate, dibutyl maleate, dioctyl maleate, vinyl acetate, vinyl propionate, and the like. These monomers may be used in combination of two or more.
架橋用ビニルモノマーのうち多官能性炭化水素系単量体
には、ジビニルベンゼン及びその誘導体、シクロペンタ
ジェン、ブタジェン等のジエン系化合物、ジビニルエス
テル化合物、ジビニルウレタン化合物等が包含される。Among the vinyl monomers for crosslinking, polyfunctional hydrocarbon monomers include divinylbenzene and derivatives thereof, diene compounds such as cyclopentadiene and butadiene, divinyl ester compounds, divinyl urethane compounds, and the like.
これらの多官能性炭化水素系単量体としては前述の単官
能性誘導体と共重合し得る化合物でなくてはならず、均
一な共重合物をつくるものが特に好ましい。These polyfunctional hydrocarbon monomers must be compounds that can be copolymerized with the above-mentioned monofunctional derivatives, and those that form a uniform copolymer are particularly preferred.
以上述べた側鎖二重結合型樹脂と前記架橋用ビニルモノ
マーとを主成分とする含浸樹脂液を用い、第1図に示し
た装置とプロセスを利用して積層板を連続的に製造した
。Using an impregnating resin solution containing the above-mentioned side chain double bond type resin and the crosslinking vinyl monomer as main components, a laminate was continuously manufactured using the apparatus and process shown in FIG. 1.
紙基材1は夫々脱湿処理又はメラミン樹脂等による前処
理の装置2を通り、側鎖二重結合型樹脂と架橋用ビニル
モノマーからなる樹脂含浸装置3において基材内に十分
樹脂液が供給される。この樹脂液含浸紙基材6は重ねあ
わせるローラー7上にて一体化され、所望量の含浸樹脂
液の排除を行い、その重なった樹脂液含浸基材を直ちに
含浸液浴8a内に浸漬して設けた液中絞りローラー8に
導き、含浸液中で加圧し、これを抽き出して得た積層体
Aをローラー7上を通って加熱用オーブン9中に送られ
る。該オーブン中では加圧ロール11゜11その他通常
用いられる加圧装置で加圧され、含浸液の所望量の排除
を行いつつ加熱硬化され積層板13が得られる。なお、
積層体Aを加熱用オーブン中に送りこむに際し、金属箔
にも同時に引き込み、金属張り積層板をつくることがで
きる。The paper base material 1 passes through a device 2 for dehumidification treatment or pretreatment with melamine resin, etc., and a resin impregnation device 3 consisting of a side chain double bond type resin and a crosslinking vinyl monomer supplies enough resin liquid into the base material. be done. The resin liquid-impregnated paper base materials 6 are combined on a roller 7 to be overlapped, a desired amount of the impregnated resin liquid is removed, and the overlapping resin liquid-impregnated base materials are immediately immersed in an impregnating liquid bath 8a. The laminate A is introduced into the submerged squeezing roller 8 provided, pressurized in the impregnating liquid, and extracted. The resulting laminate A is passed over the roller 7 and sent into the heating oven 9. In the oven, pressure is applied using pressure rolls 11.degree. 11 and other commonly used pressure devices, and the laminate 13 is heated and cured while removing a desired amount of the impregnating liquid. In addition,
When the laminate A is sent into a heating oven, a metal foil can also be drawn in at the same time to create a metal-clad laminate.
次に実施例にて本発明を説明する。Next, the present invention will be explained with reference to Examples.
[実 施 例]
樹脂含浸液として、前記(1)の方法により製造された
前記(1)型側鎖を有する側鎖二重結合型樹脂を用い、
厚さ300μ、表面粗さ20μRMS程度のクラフト紙
を用い含浸樹脂液粘度、50センチポイズのものを用い
、含浸後5枚を重ねて積層体とし、約5 kg / c
rnO線圧のもとてこれを固液を入れた含浸浴でかつ液
中に浸漬された直径150mmの絞りロールを通して加
圧してからとり出し、加熱オーブン中で約1.0kg/
cm線圧の加圧ローラー群(10対)を通し、前半では
含浸液の排除を行いつつ硬化させて積層板を得た。成形
速度は3m/分である。[Example] Using the side chain double bond type resin having the type (1) type side chain produced by the method (1) above as the resin impregnating liquid,
Use kraft paper with a thickness of 300μ and a surface roughness of about 20μRMS and an impregnated resin liquid with a viscosity of 50 centipoise.After impregnation, 5 sheets are stacked to form a laminate, and the weight is approximately 5 kg/c.
It was pressurized under rnO linear pressure through an impregnating bath containing a solid liquid and a squeezing roll with a diameter of 150 mm immersed in the liquid, and then taken out and placed in a heating oven at a weight of about 1.0 kg/kg.
A laminate was obtained by passing through a group of pressurizing rollers (10 pairs) with cm line pressure and curing while removing the impregnating liquid in the first half. The molding speed is 3 m/min.
該得られた積層板の断面を観察した結果、基材内には含
浸樹脂は存在するが樹脂間には殆どないことが観察され
た。As a result of observing the cross section of the obtained laminate, it was observed that although the impregnated resin was present in the base material, there was hardly any between the resins.
[比 較 例コ
側鎖二重結合型樹脂の代りに不飽和ポリエステル樹脂を
用いる以外実施例と同じ条件で積層板を作成しようとし
たが加熱オーブン中の加圧で基材から含浸樹脂液が流出
してしまい積層板が得られなかった。[Comparative Example] An attempt was made to create a laminate under the same conditions as in Example except that an unsaturated polyester resin was used instead of the side chain double bond type resin, but the impregnating resin liquid was removed from the base material due to the pressure in the heating oven. It flowed out and a laminate could not be obtained.
以上述べたごとく、本発明は従来広く用いられている。As described above, the present invention has been widely used in the past.
たとえばフェノール樹脂を用いた加熱プレスによるバッ
チ方式によって生産されている積層板やその金属箔張り
積層板において好ましい圧力を確保できない為に不可能
であった連続生産方式を、前記したごとき適切な硬化性
樹脂液と基材を用いることにより工業的に実現可能な成
型方法により高能率でかつ良好な品質を有する積層板や
金属箔張り積層板の連続生産を可能としたものであり、
その工業的価値は極めて大きい。For example, the continuous production method that was impossible due to the inability to secure the appropriate pressure for laminates and metal foil-clad laminates produced by a batch method using a hot press using phenolic resin, has been made possible by the above-mentioned suitable hardening properties. By using a resin liquid and a base material, it is possible to continuously produce laminates and metal foil-clad laminates with high efficiency and good quality using an industrially feasible molding method.
Its industrial value is extremely large.
第1図は本発明の金属箔張り積層板の製造装置とプロセ
スの一例の概略図である。
1は紙基材、2は紙基材の脱湿前処理装置、3は含浸装
置、4は硬化性樹脂液タンク、5は樹脂液移送ポンプ、
6は樹脂液含浸紙基材、7はガイドロール、8は液中絞
りロール、9は加熱用オーΦ
ブン、10はラミネート用金属箔、11は加圧多ロール
、12は切断機、13は積層板である。FIG. 1 is a schematic diagram of an example of an apparatus and process for manufacturing a metal foil-clad laminate according to the present invention. 1 is a paper base material, 2 is a dehumidification pre-treatment device for paper base materials, 3 is an impregnation device, 4 is a curable resin liquid tank, 5 is a resin liquid transfer pump,
6 is a paper base material impregnated with resin liquid, 7 is a guide roll, 8 is a submerged squeezing roll, 9 is a heating oven, 10 is a metal foil for lamination, 11 is a pressurized multi-roll, 12 is a cutting machine, 13 is a It is a laminated board.
Claims (1)
を連続的に含浸させた後その複数枚を重ねあわせた状態
で再度同一含浸樹脂液中に導き、該液内の絞りローラー
を通してからひき出し、加圧下に余剰含浸樹脂液を排出
させつつ加熱硬化する積層板の連続的製造方法。After continuously impregnating a paper base material with a resin composition whose main component is a side chain double bond type resin, multiple sheets are stacked and introduced into the same impregnated resin solution again, and the aqueous squeezing process is carried out. A continuous method for manufacturing a laminate, in which it is passed through a roller, pulled out, and heated and cured while draining excess impregnated resin liquid under pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63116515A JPH01286850A (en) | 1988-05-13 | 1988-05-13 | Continuous manufacture of laminate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63116515A JPH01286850A (en) | 1988-05-13 | 1988-05-13 | Continuous manufacture of laminate |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01286850A true JPH01286850A (en) | 1989-11-17 |
Family
ID=14689054
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63116515A Pending JPH01286850A (en) | 1988-05-13 | 1988-05-13 | Continuous manufacture of laminate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01286850A (en) |
-
1988
- 1988-05-13 JP JP63116515A patent/JPH01286850A/en active Pending
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