JPH04170444A - Expanded plastics and its production - Google Patents
Expanded plastics and its productionInfo
- Publication number
- JPH04170444A JPH04170444A JP29538590A JP29538590A JPH04170444A JP H04170444 A JPH04170444 A JP H04170444A JP 29538590 A JP29538590 A JP 29538590A JP 29538590 A JP29538590 A JP 29538590A JP H04170444 A JPH04170444 A JP H04170444A
- Authority
- JP
- Japan
- Prior art keywords
- formula
- weight
- polymer
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- tert
- 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
- 229920003023 plastic Polymers 0.000 title claims abstract description 8
- 239000004033 plastic Substances 0.000 title claims abstract description 8
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 229920000642 polymer Polymers 0.000 claims abstract description 22
- 229920001577 copolymer Polymers 0.000 claims abstract description 13
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical group CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229920001519 homopolymer Polymers 0.000 claims abstract description 5
- 239000011342 resin composition Substances 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 15
- 238000010521 absorption reaction Methods 0.000 claims description 13
- 239000000178 monomer Substances 0.000 claims description 13
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims description 11
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 7
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 claims description 5
- 230000000379 polymerizing effect Effects 0.000 claims description 4
- 239000003505 polymerization initiator Substances 0.000 claims description 3
- ISXSCDLOGDJUNJ-UHFFFAOYSA-N tert-butyl prop-2-enoate Chemical compound CC(C)(C)OC(=O)C=C ISXSCDLOGDJUNJ-UHFFFAOYSA-N 0.000 claims description 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 2
- GYCMBHHDWRMZGG-UHFFFAOYSA-N Methylacrylonitrile Chemical compound CC(=C)C#N GYCMBHHDWRMZGG-UHFFFAOYSA-N 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims 3
- 125000002914 sec-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims 1
- 239000004604 Blowing Agent Substances 0.000 abstract description 12
- 150000008360 acrylonitriles Chemical group 0.000 abstract 1
- 239000006260 foam Substances 0.000 description 20
- 239000000463 material Substances 0.000 description 16
- 229920005989 resin Polymers 0.000 description 12
- 239000011347 resin Substances 0.000 description 12
- SJMYWORNLPSJQO-UHFFFAOYSA-N tert-butyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC(C)(C)C SJMYWORNLPSJQO-UHFFFAOYSA-N 0.000 description 10
- 238000006116 polymerization reaction Methods 0.000 description 9
- 239000006261 foam material Substances 0.000 description 7
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 6
- 229920000058 polyacrylate Polymers 0.000 description 5
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 4
- 239000004800 polyvinyl chloride Substances 0.000 description 4
- 229920000915 polyvinyl chloride Polymers 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 3
- 239000007870 radical polymerization initiator Substances 0.000 description 3
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004342 Benzoyl peroxide Substances 0.000 description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 2
- ATHHXGZTWNVVOU-UHFFFAOYSA-N N-methylformamide Chemical compound CNC=O ATHHXGZTWNVVOU-UHFFFAOYSA-N 0.000 description 2
- 239000004642 Polyimide Substances 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 125000002560 nitrile group Chemical group 0.000 description 2
- 229920001721 polyimide Polymers 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 238000010557 suspension polymerization reaction Methods 0.000 description 2
- PQUXFUBNSYCQAL-UHFFFAOYSA-N 1-(2,3-difluorophenyl)ethanone Chemical compound CC(=O)C1=CC=CC(F)=C1F PQUXFUBNSYCQAL-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- 101100459896 Caenorhabditis elegans ncl-1 gene Proteins 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229920000271 Kevlar® Polymers 0.000 description 1
- 229920005830 Polyurethane Foam Polymers 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 239000011358 absorbing material Substances 0.000 description 1
- 229940048053 acrylate Drugs 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 125000000751 azo group Chemical group [*]N=N[*] 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical group CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000004918 carbon fiber reinforced polymer Substances 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000011162 core material Substances 0.000 description 1
- OIWOHHBRDFKZNC-UHFFFAOYSA-N cyclohexyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC1CCCCC1 OIWOHHBRDFKZNC-UHFFFAOYSA-N 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000004761 kevlar Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 229920007790 polymethacrylimide foam Polymers 0.000 description 1
- 229920006327 polystyrene foam Polymers 0.000 description 1
- 239000011496 polyurethane foam Substances 0.000 description 1
- 239000012783 reinforcing fiber Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229940047670 sodium acrylate Drugs 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- OPQYOFWUFGEMRZ-UHFFFAOYSA-N tert-butyl 2,2-dimethylpropaneperoxoate Chemical compound CC(C)(C)OOC(=O)C(C)(C)C OPQYOFWUFGEMRZ-UHFFFAOYSA-N 0.000 description 1
- VXHFNALHLRWIIU-UHFFFAOYSA-N tert-butyl 2,2-dimethylpropanoate Chemical compound CC(C)(C)OC(=O)C(C)(C)C VXHFNALHLRWIIU-UHFFFAOYSA-N 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、加熱することにより得られるポリ(メタ)ア
クリルイミドフオーム(メタアクリルイミドフオームあ
るいはアクリルイミドフオームを示す。以下同様に記す
。)に変換した耐熱性でかつ低吸水性の発泡プラスチッ
クスに関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to poly(meth)acrylimide foam (methacrylimide foam or acrylimide foam, hereinafter referred to in the same manner) obtained by heating. This invention relates to converted foamed plastics that are heat resistant and have low water absorption.
〔従来の技術及び発明が解決し、ようとする課題〕従来
より断熱材あるいは防音材として利用される発泡材料と
してはポリウレタン発泡体、ポリスチレン発泡体、ポリ
塩化ビニル発泡体等の熱可塑樹脂を用いた発泡体が知ら
れている。近年これらの発泡材料が飛行機、船舶等の構
造材料、すなわち複合材料サンドイツチ板のコア材とし
て用いられようとしている。これは従来より用いられて
いるハニカム構造体の接着あるいは補修の困難さに依る
ものである。しかし従来の発泡材料ではサンドイッチ構
造体の成形温度あるいは成形圧力に耐えられなかった。[Problems to be solved by the prior art and the invention] Thermoplastic resins such as polyurethane foam, polystyrene foam, and polyvinyl chloride foam have traditionally been used as foam materials for heat insulation or sound insulation. Foams are known. In recent years, these foamed materials have been used as structural materials for airplanes, ships, etc., ie, as core materials for composite sandwich boards. This is due to the difficulty in adhering or repairing conventionally used honeycomb structures. However, conventional foam materials cannot withstand the molding temperatures or pressures of sandwich structures.
これらの問題に対して種々の検討が行われている。例え
ば特公昭51−50219号、特公昭61−36532
号あるいは特公昭61−36534号公報には、(メタ
)アクリロニトリルと(メタ)アクリル酸を発泡剤、例
えば低級アルコール、ホルムアミド、モノメチルホルム
アミド等とともに共重合させた樹脂板を180〜220
℃で加熱発泡し、同時にイミド化した耐熱性ポリイミド
発泡材料が記載されている。これらの発泡材料は密度0
、03〜0.2 g/cm’程度と軽量で、かつ耐熱温
度180℃と通常の複合材料の成形温度に耐えうる耐熱
性を有している。しかしこれら材料の吸水特性は非常に
悪い。例えば70℃の水中に浸漬させると、50日で4
60重量%という著しい重量増加を示す。これはポリウ
レタン、ポリ塩化ビニル製発泡材料が、同条件で吸水さ
せた場合、数十%しか重量増加しないのに比べて10倍
以上と著しく高い。このため発泡前の樹脂板、発泡体と
もに吸湿が大きく、室温に保管した場合、使用前に乾燥
する必要がある。これに対し特開昭61−272247
号公報には、吸湿性を改善したポリイミド発泡材料が記
載されている。これらの材料は低吸湿性のため通常の室
温条件での保存が可能であり、70℃水中浸漬では50
日で325重量%増加と従来品より低くなっているが、
ポリウレタン、ポリ塩化ビニル製発泡体に比較するとま
だ高レベルにある。またいづれの材料も低沸点の低級ア
ルコール、ホルムアミド等の発泡材と共に重合させるた
め、重合温度を上げられず、40〜60℃で20〜40
時間と低温、長時間を要するため、生産性、経済性の点
でも問題があった。Various studies are being conducted on these issues. For example, Special Publication No. 51-50219, Special Publication No. 61-36532
No. 61-36534 discloses a resin plate made by copolymerizing (meth)acrylonitrile and (meth)acrylic acid with a blowing agent such as lower alcohol, formamide, monomethylformamide, etc.
A heat-resistant polyimide foam material is described that is heated and foamed at °C and simultaneously imidized. These foam materials have a density of 0
, about 03 to 0.2 g/cm', and has a heat resistance of 180°C, which can withstand the molding temperature of ordinary composite materials. However, the water absorption properties of these materials are very poor. For example, if immersed in water at 70℃, 4
It shows a significant weight increase of 60% by weight. This is significantly higher than that of polyurethane and polyvinyl chloride foam materials, which increase in weight by only several tens of percent when water is absorbed under the same conditions. For this reason, both the resin board and the foam before foaming absorb a lot of moisture, and if stored at room temperature, it is necessary to dry them before use. On the other hand, JP-A-61-272247
The publication describes a polyimide foam material with improved hygroscopicity. These materials have low hygroscopicity and can be stored at normal room temperature, and when immersed in water at 70°C,
This is a 325% weight increase per day, which is lower than conventional products, but
This is still at a high level compared to polyurethane and polyvinyl chloride foams. Furthermore, since both materials are polymerized together with foaming materials such as lower alcohols and formamide, which have low boiling points, it is not possible to raise the polymerization temperature;
Because it requires time, low temperature, and long hours, there are also problems in terms of productivity and economy.
本発明者らは、前記の問題について種々検討した結果、
発泡剤として(メタ)アクリル酸ターシャルブチル重合
体、メタアクリル酸ターシャルブチル−アクリル酸ター
シャルブチル共重合体のうちから選ばれる少なくとも1
種の重合体を用いることにより、高温短時間で重合し、
しかも低吸水性の耐熱性発泡材を製造できることを見出
して本発明を完成した。As a result of various studies on the above-mentioned problem, the present inventors found that
As a blowing agent, at least one selected from tert-butyl (meth)acrylate polymer and tert-butyl methacrylate-tert-butyl acrylate copolymer;
By using a seed polymer, it can be polymerized at high temperature and in a short time,
Moreover, the present invention was completed by discovering that it is possible to produce a heat-resistant foam material with low water absorption.
本発明は、次式
%式%(1)
(式中のRは水素原子又はメチル基を示す)で表される
構造単位と、次式
%式%()
(式中のRは水素原子又はメチル基を示す)で表される
構造単位の比が273〜3/2(モル比)で、かつ式(
1)及び(II)で表される構造単位の合計が少なくと
も20重量%である分子量50000〜500000の
共重合体(A) 100重量部と次式%式%()
(式中のR1は水素原子又はメチル基を示す)の構造単
位で表される分子量50000〜500000の単独重
合体及び/又は共重合体(B)1〜100重量部を含有
する、加熱することにより耐熱性でかつ低吸水性の発泡
プラスチックスと与える樹脂組成物である。The present invention combines a structural unit represented by the following formula % formula % (1) (R in the formula represents a hydrogen atom or a methyl group) and a structural unit represented by the following formula % formula % () (in the formula R represents a hydrogen atom or a methyl group). (representing a methyl group) is 273 to 3/2 (molar ratio), and the formula (
100 parts by weight of a copolymer (A) with a molecular weight of 50,000 to 500,000 in which the total of structural units represented by Contains 1 to 100 parts by weight of a homopolymer and/or copolymer (B) with a molecular weight of 50,000 to 500,000, represented by the structural unit of (atom or methyl group), which is heat resistant and has low water absorption when heated. It is a resin composition that provides flexible foamed plastics.
式(1)〜(I[[)で表される構造単位中の個々のR
及びR1は同一でも異なっていてもよい。Individual R in the structural units represented by formulas (1) to (I[[)
and R1 may be the same or different.
本発明はさらに、(メタ)アクリル酸と(メタ)アクリ
ロニトリルとの比が2/3〜3/2 (モル比)から構
成される重合性単量体混合物を少なくとも20重量%含
有する重合性単量体混合物100重量部に対しメタクリ
ル酸ターシャルブチル重合体、アクリル酸ターシャルブ
チル重合体、メタクリル酸ターシャルブチル−アクリル
酸ターシャルブチル共重合体の中から選ばれた少なくと
も1種の重合体1〜100重量部及び重合開始剤を溶解
し、50〜120℃に加熱重合して得られる共重合体を
加熱発泡させることを特徴とする耐熱性でかつ低吸水性
の発泡プラスチックスの製法である。The present invention further provides a polymerizable monomer containing at least 20% by weight of a polymerizable monomer mixture in which the ratio of (meth)acrylic acid to (meth)acrylonitrile is 2/3 to 3/2 (mole ratio). At least one polymer selected from tert-butyl methacrylate polymer, tert-butyl acrylate polymer, and tert-butyl methacrylate-tert-butyl acrylate copolymer per 100 parts by weight of the polymer mixture. 1 to 100 parts by weight and a polymerization initiator are dissolved, and a copolymer obtained by heating and polymerizing at 50 to 120°C is heated and foamed. be.
発泡プラスチックスを製造するための加熱温度は180
〜240℃が好ましい。The heating temperature for producing foamed plastics is 180℃.
~240°C is preferred.
本発明における(メタ)アクリル酸と(メタ)アクリロ
ニトリルの仕込み比は2/3〜3/2(モル比)の範囲
である。仕込みのモル比がこの範囲外の場合は各重合性
単量体が単独重合体となり易く、イミド化の反応が起こ
りにくくなる。また特に(メタ)アクリロニトリルの含
量が高くなると、側鎖のニトリル基の重合により発泡体
が黒づんだり、あるいは脆くなり易く好ましくない。The charging ratio of (meth)acrylic acid and (meth)acrylonitrile in the present invention is in the range of 2/3 to 3/2 (molar ratio). When the charged molar ratio is outside this range, each polymerizable monomer tends to form a homopolymer, making it difficult for the imidization reaction to occur. In addition, particularly when the content of (meth)acrylonitrile is high, the foam tends to darken or become brittle due to polymerization of the nitrile groups in the side chains, which is undesirable.
本発明ではこの(メタ)アクリル酸及び(メタ)アクリ
ロニトリル混合物を20重量%以上含有する重合性単量
体混合物を用いる。この含有率が20重量%未満ではイ
ミド化の割合が低くなり、得られる発泡材料の耐熱性が
低下する。In the present invention, a polymerizable monomer mixture containing 20% by weight or more of this mixture of (meth)acrylic acid and (meth)acrylonitrile is used. If this content is less than 20% by weight, the imidization rate will be low and the heat resistance of the resulting foamed material will be reduced.
この混合物に追加する重合性不飽和単量体としては(メ
タ)アクリルアミド、N−メチル(メタ)アクリルアミ
ド、(メタ)アクリル酸等の低級アルキルエステル類、
シクロヘキシル等が挙げられるが、(メタ)アクリル酸
または(メタ)アクリロニトリルと共重合可能であれば
他の不飽和重合性単量体も使用できる。Polymerizable unsaturated monomers added to this mixture include lower alkyl esters such as (meth)acrylamide, N-methyl (meth)acrylamide, and (meth)acrylic acid;
Examples include cyclohexyl, but other unsaturated polymerizable monomers can also be used as long as they are copolymerizable with (meth)acrylic acid or (meth)acrylonitrile.
本発明では発泡剤として、(メタ)アクリル酸ターシャ
ルブチルあるいはこれらの共重合体の少なくとも1種の
重合体を用いる。これは(メタ)アクリル酸ターシャル
ブチル重合体を180℃以上の温度に加熱すると、ター
シャルブチル基がイソブチンとして脱離し、このイソブ
チンが発泡剤として働くためである。本発明では発泡剤
として前記の重合体を用いることにより、種々の特徴を
有している。まずイソブチン脱離後に形成されるカルボ
キシル基は(メタ)アクリロニトリルのニトリル基と反
応して(メタ)アクリルイミド基を形成し、耐熱性の材
料になる。次に低沸点の発泡剤を用いないため、重合温
度を上げることが可能となり、重合時間が短縮でき、生
産性、経済性の点で有利になる。またイミド化の反応が
進みやすくなり、樹脂吸水性が下がり、保存安定性が向
上し、かつ吸水による特性低下も少なくなる。In the present invention, at least one polymer of tert-butyl (meth)acrylate or a copolymer thereof is used as a blowing agent. This is because when the tertiary butyl (meth)acrylate polymer is heated to a temperature of 180° C. or higher, the tertiary butyl group is eliminated as isobutyne, and this isobutyne acts as a blowing agent. The present invention has various features by using the above polymer as a blowing agent. First, the carboxyl group formed after isobutyne is eliminated reacts with the nitrile group of (meth)acrylonitrile to form a (meth)acrylimide group, resulting in a heat-resistant material. Secondly, since no blowing agent with a low boiling point is used, it becomes possible to raise the polymerization temperature and shorten the polymerization time, which is advantageous in terms of productivity and economy. In addition, the imidization reaction progresses more easily, the water absorption of the resin is reduced, the storage stability is improved, and the deterioration of properties due to water absorption is reduced.
この発泡剤である重合体は、メタアクリル酸ターシャル
ブチル及びアクリル酸ターシャルブチルを単独であるい
は両者を任意の割合で混合してラジカル重合開始剤の存
在下に50〜120℃で重合させることにより簡単に得
られる。重合の方法としては塊状重合、乳化重合、懸濁
重合いずれでもよいが、得られる重合体の取り扱い性や
溶解作業の容易なバール状の重合体の得られる懸濁重合
が好ましい。The polymer that is the blowing agent is prepared by polymerizing tert-butyl methacrylate and tert-butyl acrylate alone or by mixing the two in an arbitrary ratio at 50 to 120°C in the presence of a radical polymerization initiator. can be easily obtained by The polymerization method may be any of bulk polymerization, emulsion polymerization, and suspension polymerization, but suspension polymerization is preferred because it yields a burl-shaped polymer that is easy to handle and dissolve.
ラジカル重合開始剤としてはベンゾイルパーオキサイド
、t−ブチルパーピバレート、アゾビスイソブチロニト
リル等が好ましい。Preferred radical polymerization initiators include benzoyl peroxide, t-butyl perpivalate, azobisisobutyronitrile, and the like.
発泡剤である(メタ)アクリル酸ターシャルブチル重合
体の使用量は目的とする発泡体の密度により異なるが、
(メタ)アクリル酸及び(メタ)アクリロニトリルを含
有する重合性不飽和単量体混合物に対して1〜100重
量%、好ましくは5〜50重量%の範囲である。使用量
が1重量%未満では発泡性が不十分となり、100重量
%より多いと重合体が脆くなり好ましくない。The amount of tert-butyl (meth)acrylate polymer used as a blowing agent varies depending on the density of the desired foam.
The amount is in the range of 1 to 100% by weight, preferably 5 to 50% by weight, based on the polymerizable unsaturated monomer mixture containing (meth)acrylic acid and (meth)acrylonitrile. If the amount used is less than 1% by weight, the foamability will be insufficient, and if it is more than 100% by weight, the polymer will become brittle, which is not preferable.
本発明では(メタ)アクリル酸及び(メタ)アクリロニ
トリルを20重量%以上を含有する重合性不飽和単量体
混合物に、発泡剤である(メタ)アクリル酸ターシャル
ブチル重合体を溶解し、ラジカル重合開始剤を添加した
混合物を50〜120℃好ましくは60〜100℃の温
度に加熱して塊状重合させることにより発泡性共重合体
を得る。In the present invention, a tert-butyl (meth)acrylate polymer as a blowing agent is dissolved in a polymerizable unsaturated monomer mixture containing 20% by weight or more of (meth)acrylic acid and (meth)acrylonitrile, and a radical A foamable copolymer is obtained by bulk polymerizing the mixture to which a polymerization initiator has been added by heating to a temperature of 50 to 120°C, preferably 60 to 100°C.
発泡性共重合体は、通常は塩化ビニル製のスペーサーを
用いたガラスセルキャスト法で作成されるため、厚みは
任意に調整可能であるが、重合発熱等を考慮して重合温
度等の条件については十分な注意を払う必要がある。Expandable copolymers are usually created by the glass cell casting method using a spacer made of vinyl chloride, so the thickness can be adjusted arbitrarily, but conditions such as polymerization temperature must be adjusted in consideration of polymerization heat generation, etc. requires sufficient attention.
本発明の組成物は高温、短時間の重合が可能であるため
、ステンレスベルトを用いた連続製板法で製造すること
もできる。Since the composition of the present invention can be polymerized at high temperatures and in a short time, it can also be manufactured by a continuous sheet-making method using a stainless steel belt.
ラジカル重合開始剤としてはベンゾイルパーオキサイド
、t−ブチルピバレート等の過酸化物、アゾビスイソブ
チロニトリル等のアゾ化合物が好ましい。As the radical polymerization initiator, peroxides such as benzoyl peroxide and t-butyl pivalate, and azo compounds such as azobisisobutyronitrile are preferred.
こうして得られる共重合体は180〜240℃に加熱す
ることにより発泡し、5〜20倍発泡で0.05〜0.
25 g/cm3の密−度が得られる。また得られる発
泡体は約180℃までの耐熱性を有する。The copolymer thus obtained is foamed by heating to 180 to 240°C, and foams 5 to 20 times by 0.05 to 0.
A density of 25 g/cm3 is obtained. The resulting foam also has heat resistance up to about 180°C.
本発明による発泡材料は単独で耐熱用途の断熱材、吸音
材として用いられるほか板状発泡材料の両面を熱硬化性
樹脂を含浸した強化繊維補強材料いわゆるプリプレグで
サンドイッチした材料を硬化させた構造体として有利り
使用可能である。強化繊維としては炭素繊維、ガラス繊
維、ケブラー(登録商標)等の有機繊維のいずれでも使
用可能である。The foamed material according to the present invention can be used alone as a heat-resistant heat insulating material or a sound absorbing material, and can also be used as a structure made by hardening a plate-shaped foamed material sandwiched between both sides of a reinforced fiber reinforced material called prepreg impregnated with a thermosetting resin. It can be advantageously used as As the reinforcing fiber, any organic fiber such as carbon fiber, glass fiber, or Kevlar (registered trademark) can be used.
以下、実施例により本発明をさらに詳細に説明する。な
お実施例では重合性単量体を下記の略号で示す。Hereinafter, the present invention will be explained in more detail with reference to Examples. In the examples, polymerizable monomers are indicated by the following abbreviations.
メタクリル@ : MAA
アクリル酸 :AA
メタクリロニトリル:MAN
アクリロニトリル:AN
メタクリル酸ターシャルブチル:TBMAアクリル酸タ
ーシャルブチル: TBA参考例I
TBMA単独重合体の製造:
発泡剤として用いるTBMA重合体を以下の手順に従っ
て製造した。イオン交換水100部、分散安定剤として
アクリル酸ナトリウム0.2部及び硫酸ナトリウム0.
15部を窒素置換したセパラブルフラスコに入れて攪拌
し、分散安定剤及び硫酸ナトリウムを溶解させる。別に
TBMAI 00部にアゾビスイソブチロニトリル0.
1部を溶解させ、これを前記のセパラブルフラスコに投
入する。投入後、激しく攪拌し、千ツマ−を水中に分散
させた状態で加熱を開始する。浴温を確認しつつ加熱を
続けた。内温か一定(77℃)になってから90分後に
重合の発熱ピークを生じた。ピーク(83℃)が出てか
ら約30分間加熱を続け、重合を完結させて加熱を止め
た。得られたビーズ状の重合体をイオン交換水を用いて
洗浄したのち、60℃で加熱乾燥することによりTBM
A重合体を得た。Methacrylic @: MAA Acrylic acid: AA Methacrylonitrile: MAN Acrylonitrile: AN Tertiary butyl methacrylate: TBMA Tertiary butyl acrylate: TBA Reference Example I Production of TBMA homopolymer: The TBMA polymer used as a blowing agent was prepared as follows. Manufactured according to the procedure. 100 parts of ion-exchanged water, 0.2 parts of sodium acrylate and 0.2 parts of sodium sulfate as dispersion stabilizers.
15 parts were placed in a separable flask purged with nitrogen and stirred to dissolve the dispersion stabilizer and sodium sulfate. Separately, 0.00 parts of TBMAI and 0.00 parts of azobisisobutyronitrile.
One part of the solution was dissolved and put into the above-mentioned separable flask. After adding the water, stir vigorously and start heating with the water dispersed in the water. Heating was continued while checking the bath temperature. An exothermic peak of polymerization occurred 90 minutes after the internal temperature became constant (77°C). Heating was continued for about 30 minutes after the peak (83°C) appeared, and heating was stopped after polymerization was completed. After washing the obtained bead-shaped polymer with ion-exchanged water, TBM was prepared by heating and drying at 60°C.
Polymer A was obtained.
実施例1
MAA50重量部、及びMAN50重量部を均一に混合
し、参考例1で得られたTBMA重合体16重量部を加
え、室温で攪拌して溶解させた。Example 1 50 parts by weight of MAA and 50 parts by weight of MAN were uniformly mixed, 16 parts by weight of the TBMA polymer obtained in Reference Example 1 was added, and the mixture was stirred and dissolved at room temperature.
均一溶解後、アゾピスイソブチロニ) ジル2重量部を
溶解させた。この均一溶解物を2枚のガラス板の間にポ
リ塩化ビニルスペーサーを挟んだセルの間に流し込み、
80℃で2時間加熱して硬化させると、不透明な樹脂板
が得られた。After uniform dissolution, 2 parts by weight of azopisisobutyronidine was dissolved. This homogeneous melt was poured into a cell with a polyvinyl chloride spacer sandwiched between two glass plates.
When the resin was cured by heating at 80° C. for 2 hours, an opaque resin plate was obtained.
この樹脂を200℃で2時間加熱することにより、0゜
06g/cm’の密度を有するポリメタクリルイミドフ
オームを得た。また同じ樹脂板を220℃で2時間加熱
することにより、0.04 g/cm’の密度を有する
発泡材料を得た。By heating this resin at 200°C for 2 hours, a polymethacrylimide foam having a density of 0°06 g/cm' was obtained. Further, by heating the same resin plate at 220°C for 2 hours, a foamed material having a density of 0.04 g/cm' was obtained.
得られた発泡材料を長さ100mmX幅100mm×厚
み25mmに切断し、70℃で48時間乾燥した後、7
0tX95%RHで吸湿試験を実施したところ、2日で
吸湿量は飽和し、3.5%の重量増加を示した。発泡体
密度による吸水量の差はほとんどなかった。The obtained foamed material was cut into pieces of length 100 mm x width 100 mm x thickness 25 mm, dried at 70°C for 48 hours, and then
When a moisture absorption test was conducted at 0t x 95% RH, the moisture absorption amount was saturated in 2 days and a weight increase of 3.5% was observed. There was almost no difference in water absorption depending on foam density.
実施例2及び比較例1
発泡剤であるTBMA重合体量を変えた以外は実施例1
と同様にして樹脂板を得た。この樹脂板を200℃で2
時間加熱することにより、表1に示す各種密度を有する
発泡材料を得た。表中のTBMA重合体添加量は、MA
A50重量部及びMAN50重量部の混合物に対する添
加量を意味する。Example 2 and Comparative Example 1 Example 1 except that the amount of TBMA polymer as a blowing agent was changed.
A resin plate was obtained in the same manner. This resin plate was heated to 200℃ for 2 hours.
By heating for a period of time, foamed materials having various densities shown in Table 1 were obtained. The amount of TBMA polymer added in the table is MA
It means the amount added to a mixture of 50 parts by weight of A and 50 parts by weight of MAN.
表 1
実験NCL 1及び6はTBMA重合体添加量は本発明
の範囲外である組成物を用いた例である。これら実験で
得られた材料に比べ、本発明の範囲である実験N112
〜50発泡体は均一に発泡し、吸湿量も低い材料である
ことがわかる。Table 1 Experiments NCL 1 and 6 are examples using compositions in which the amount of TBMA polymer added is outside the range of the present invention. Compared to the materials obtained in these experiments, experiment N112, which is within the scope of the present invention,
It can be seen that the ~50 foam is a material that foams uniformly and has a low amount of moisture absorption.
実施例3
実施例1で得られた発泡材料を100IIIIl×11
0011111X25に切断し、70℃で48時間乾燥
を実施した。この発泡体の長さ、輻及び厚みを正確に測
定した後、180℃で2時間加熱して発泡体寸法を測定
した。加熱前後の発泡体の寸法変形はいづれも1岨以下
であり、通常のCFRPサンドイッチ板の硬化温度に耐
えうろことがわかる。Example 3 The foamed material obtained in Example 1 was mixed into 100III1×11
It was cut into 0011111×25 pieces and dried at 70° C. for 48 hours. After accurately measuring the length, radius and thickness of this foam, it was heated at 180° C. for 2 hours and the dimensions of the foam were measured. The dimensional deformation of the foam before and after heating was less than 1 dimensional, indicating that it could withstand the curing temperature of ordinary CFRP sandwich boards.
実施例4
重合性単量体としてMAA30重量部、MAN40重量
部及びメタクリル酸シクロヘキシル30加、攪拌して均
一な重合性単量体混合物を得た。Example 4 30 parts by weight of MAA, 40 parts by weight of MAN and 30 parts by weight of cyclohexyl methacrylate were added as polymerizable monomers and stirred to obtain a homogeneous polymerizable monomer mixture.
この混合物を実施例1と同様にして製板することにより
、乳白色の樹脂板を得た。得られた樹脂板を200℃で
2時間加熱することにより、密度0、05 g/cn+
3の均一な発泡体を得た。本発泡体を実施例1と同様に
して乾燥吸湿させた。吸水量は2.6重量%であり、さ
らに低吸水性の発泡体が得られた。A milky white resin board was obtained by making a board from this mixture in the same manner as in Example 1. By heating the obtained resin plate at 200°C for 2 hours, the density becomes 0.05 g/cn+
A uniform foam of No. 3 was obtained. This foam was dried and moisture-absorbed in the same manner as in Example 1. The water absorption amount was 2.6% by weight, and a foam with low water absorption was obtained.
出願人 三菱レイヨン株式会社 〃 三菱重工業株式会社 代理人 弁理士 高 橋 淳 −Applicant: Mitsubishi Rayon Co., Ltd. 〃 Mitsubishi Heavy Industries, Ltd Agent: Patent Attorney Atsushi Takahashi -
Claims (1)
構造単位と、次式 ▲数式、化学式、表等があります▼(II) (式中のRは水素原子又はメチル基を示す)で表される
構造単位の比が2/3〜3/2(モル比)で、かつ式(
I )及び式(II)で表される構造単位の合計が少なく
とも20重量%である分子量50000〜500000
の重合体(A)100重量部と次式▲数式、化学式、表
等があります▼(III) (式中のR^1は水素原子又はメチル基を示す)の構造
単位で表される分子量50000〜500000の単独
重合体及び/又は共重合体(B)1〜100重量部を含
有する、加熱することにより耐熱性でかつ低吸水性の発
泡プラスチックスを与える樹脂組成物。 (2)メタアクリル酸及び/又はアクリル酸とメタアク
リロニトリル及び/又はアクリロニトリルとの比が2/
3〜3/2(モル比)から構成される重合性単量体混合
物を少なくとも20重量%含有する重合性単量体混合物
100重量部に対しメタクリル酸ターシャルブチル重合
体、アクリル酸ターシヤルブチル重合体、メタクリル酸
ターシャルブチル−アクリル酸ターシャルブチル共重合
体の中から選ばれた少なくとも1種の重合体1〜100
重量部及び重合開始剤を溶解し、50〜120℃に加熱
重合して得られる共重合体を加熱することを特徴とする
耐熱性でかつ低吸水性の発泡プラスチックスの製造。 (3)加熱温度が180〜240℃であることを特徴と
する請求項2記載の方法。[Claims] A structural unit represented by the following formula ▲ Numerical formula, chemical formula, table, etc. ▼ (I) (R in the formula represents a hydrogen atom or a methyl group) and the following formula ▲ Numerical formula, chemical formula, There are tables, etc. ▼ (II) (R in the formula represents a hydrogen atom or a methyl group) The ratio of the structural units represented by the formula is 2/3 to 3/2 (molar ratio), and the formula (
I) and a molecular weight of 50,000 to 500,000 in which the sum of the structural units represented by formula (II) is at least 20% by weight
100 parts by weight of polymer (A) and the following formula ▲ Numerical formula, chemical formula, table, etc. ▼ (III) (R^1 in the formula represents a hydrogen atom or a methyl group) Molecular weight 50,000 expressed by the structural unit A resin composition containing 1 to 100 parts by weight of a homopolymer and/or a copolymer (B) of 500,000 to 500,000, which gives a heat-resistant and low water absorption foamed plastic when heated. (2) The ratio of methacrylic acid and/or acrylic acid to methacrylonitrile and/or acrylonitrile is 2/
Tert-butyl methacrylate polymer, tert-butyl acrylate to 100 parts by weight of a polymerizable monomer mixture containing at least 20% by weight of a polymerizable monomer mixture composed of 3 to 3/2 (molar ratio). At least one polymer selected from polymers, tert-butyl methacrylate-tert-butyl acrylate copolymers 1 to 100
1. Production of heat-resistant and low water-absorbing foamed plastics, which is characterized by heating a copolymer obtained by dissolving parts by weight and a polymerization initiator and polymerizing by heating at 50 to 120°C. (3) The method according to claim 2, wherein the heating temperature is 180 to 240°C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29538590A JPH04170444A (en) | 1990-11-02 | 1990-11-02 | Expanded plastics and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29538590A JPH04170444A (en) | 1990-11-02 | 1990-11-02 | Expanded plastics and its production |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04170444A true JPH04170444A (en) | 1992-06-18 |
Family
ID=17819944
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29538590A Pending JPH04170444A (en) | 1990-11-02 | 1990-11-02 | Expanded plastics and its production |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04170444A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015025069A (en) * | 2013-07-26 | 2015-02-05 | 積水化成品工業株式会社 | Acrylic resin foam |
-
1990
- 1990-11-02 JP JP29538590A patent/JPH04170444A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015025069A (en) * | 2013-07-26 | 2015-02-05 | 積水化成品工業株式会社 | Acrylic resin foam |
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