JPS63125531A - Carbon fiber-reinforced resin composition - Google Patents
Carbon fiber-reinforced resin compositionInfo
- Publication number
- JPS63125531A JPS63125531A JP26989586A JP26989586A JPS63125531A JP S63125531 A JPS63125531 A JP S63125531A JP 26989586 A JP26989586 A JP 26989586A JP 26989586 A JP26989586 A JP 26989586A JP S63125531 A JPS63125531 A JP S63125531A
- Authority
- JP
- Japan
- Prior art keywords
- pps
- carbon fiber
- ppss
- polyphenylene sulfide
- block copolymer
- 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.)
- Granted
Links
- 239000011342 resin composition Substances 0.000 title claims abstract description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title abstract 2
- 229910052799 carbon Inorganic materials 0.000 title abstract 2
- 239000004734 Polyphenylene sulfide Substances 0.000 claims abstract description 50
- 229920000069 polyphenylene sulfide Polymers 0.000 claims abstract description 50
- 229920000049 Carbon (fiber) Polymers 0.000 claims abstract description 26
- 239000004917 carbon fiber Substances 0.000 claims abstract description 26
- 229920001400 block copolymer Polymers 0.000 claims abstract description 17
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000000203 mixture Substances 0.000 claims abstract description 11
- 150000003457 sulfones Chemical class 0.000 claims abstract description 9
- 229920005989 resin Polymers 0.000 abstract description 25
- 239000011347 resin Substances 0.000 abstract description 25
- 239000004918 carbon fiber reinforced polymer Substances 0.000 abstract description 14
- 239000000126 substance Substances 0.000 abstract description 10
- 230000006866 deterioration Effects 0.000 abstract description 4
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000004033 plastic Substances 0.000 abstract 1
- 229920003023 plastic Polymers 0.000 abstract 1
- 229920000642 polymer Polymers 0.000 description 30
- 238000000034 method Methods 0.000 description 20
- 238000007334 copolymerization reaction Methods 0.000 description 11
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 239000000047 product Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- 238000006116 polymerization reaction Methods 0.000 description 7
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 6
- 229920001577 copolymer Polymers 0.000 description 6
- -1 heat resistance Substances 0.000 description 6
- 239000011159 matrix material Substances 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 6
- OCJBOOLMMGQPQU-UHFFFAOYSA-N 1,4-dichlorobenzene Chemical compound ClC1=CC=C(Cl)C=C1 OCJBOOLMMGQPQU-UHFFFAOYSA-N 0.000 description 5
- JTPNRXUCIXHOKM-UHFFFAOYSA-N 1-chloronaphthalene Chemical compound C1=CC=C2C(Cl)=CC=CC2=C1 JTPNRXUCIXHOKM-UHFFFAOYSA-N 0.000 description 5
- 229910052979 sodium sulfide Inorganic materials 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 150000001491 aromatic compounds Chemical class 0.000 description 4
- 238000004132 cross linking Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000012046 mixed solvent Substances 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- JFDZBHWFFUWGJE-UHFFFAOYSA-N benzonitrile Chemical compound N#CC1=CC=CC=C1 JFDZBHWFFUWGJE-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 239000002798 polar solvent Substances 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- GPAPPPVRLPGFEQ-UHFFFAOYSA-N 4,4'-dichlorodiphenyl sulfone Chemical compound C1=CC(Cl)=CC=C1S(=O)(=O)C1=CC=C(Cl)C=C1 GPAPPPVRLPGFEQ-UHFFFAOYSA-N 0.000 description 2
- DLFVBJFMPXGRIB-UHFFFAOYSA-N Acetamide Chemical compound CC(N)=O DLFVBJFMPXGRIB-UHFFFAOYSA-N 0.000 description 2
- KWOLFJPFCHCOCG-UHFFFAOYSA-N Acetophenone Chemical compound CC(=O)C1=CC=CC=C1 KWOLFJPFCHCOCG-UHFFFAOYSA-N 0.000 description 2
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 2
- ATHHXGZTWNVVOU-UHFFFAOYSA-N N-methylformamide Chemical compound CNC=O ATHHXGZTWNVVOU-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910052977 alkali metal sulfide Inorganic materials 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 238000006482 condensation reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 2
- 239000003822 epoxy resin Substances 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 150000003951 lactams Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 2
- 229920002492 poly(sulfone) Polymers 0.000 description 2
- 229920000647 polyepoxide Polymers 0.000 description 2
- 229920002959 polymer blend Polymers 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000012783 reinforcing fiber Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000004227 thermal cracking Methods 0.000 description 2
- AVQQQNCBBIEMEU-UHFFFAOYSA-N 1,1,3,3-tetramethylurea Chemical compound CN(C)C(=O)N(C)C AVQQQNCBBIEMEU-UHFFFAOYSA-N 0.000 description 1
- ZFPGARUNNKGOBB-UHFFFAOYSA-N 1-Ethyl-2-pyrrolidinone Chemical compound CCN1CCCC1=O ZFPGARUNNKGOBB-UHFFFAOYSA-N 0.000 description 1
- WKFQMDFSDQFAIC-UHFFFAOYSA-N 2,4-dimethylthiolane 1,1-dioxide Chemical compound CC1CC(C)S(=O)(=O)C1 WKFQMDFSDQFAIC-UHFFFAOYSA-N 0.000 description 1
- VZXOZSQDJJNBRC-UHFFFAOYSA-N 4-chlorobenzenethiol Chemical compound SC1=CC=C(Cl)C=C1 VZXOZSQDJJNBRC-UHFFFAOYSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- ZWXPDGCFMMFNRW-UHFFFAOYSA-N N-methylcaprolactam Chemical compound CN1CCCCCC1=O ZWXPDGCFMMFNRW-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 238000000862 absorption spectrum Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 150000003857 carboxamides Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- PXJJSXABGXMUSU-UHFFFAOYSA-N disulfur dichloride Chemical compound ClSSCl PXJJSXABGXMUSU-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 description 1
- 229920006258 high performance thermoplastic Polymers 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 239000009719 polyimide resin Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920005606 polypropylene copolymer Polymers 0.000 description 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical compound O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Landscapes
- Reinforced Plastic Materials (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野〕
本発明は、炭素繊維の優れ九物性を備え念耐熱性、耐薬
品性ならびに機械的強度等に優れた炭素繊維強化グラス
チック(以下CFRPと略す)′VC関する。さらに詳
しくは、ポリフェニレンスルフィド〔以下PPSと略す
〕にソフトセグメントとしてポリフェニレンスルフィド
スルホン(以下、 PP5S 、!:略す)を化学的に
結合せしめてなる共重合体を必須成分とする樹脂組成物
全含浸してなる耐熱性、耐薬品性ならびに可撓性等の機
械的性質に優れ念CFRPに関するものである。Detailed Description of the Invention (Field of Industrial Application) The present invention is directed to carbon fiber reinforced glass (hereinafter referred to as CFRP), which has the excellent physical properties of carbon fiber and has excellent heat resistance, chemical resistance, mechanical strength, etc. VC).More specifically, the essential component is a copolymer made by chemically bonding polyphenylene sulfide (hereinafter referred to as PPS) with polyphenylene sulfide sulfone (hereinafter referred to as PP5S) as a soft segment. It relates to CFRP which is completely impregnated with a resin composition and has excellent mechanical properties such as heat resistance, chemical resistance, and flexibility.
(従来の技術および問題点)
CFRPは軽量で卓越した機械的、化学的あるいは電気
的性質を有する念めに各種の構造用部材として広範囲に
使用されているが、そのCFRPをy!成する炭素繊維
とマトリックス樹脂との接着性、マトリ、クス樹脂の耐
熱性や機械的性質によりCFRPの性能は必ずしも満足
すべきものではなく、用途、例えば航空・宇宙用途等に
よってはさらに高性能のCFRPが要求されている。(Prior Art and Problems) CFRP is lightweight and has excellent mechanical, chemical, and electrical properties, so it is widely used as a variety of structural members. The performance of CFRP is not always satisfactory due to the adhesion between the carbon fibers and matrix resin, and the heat resistance and mechanical properties of the matrix and resin. is required.
このCFRPに要求される性能のうち、耐熱性や耐薬品
性等はマトリ、クス樹脂の種類に影響されるところが大
きく、例えば炭素繊維に対する接着性が良好であるエポ
キシ樹脂は耐熱性が不十分であり、一方、耐熱性に優れ
ているポリイミド樹脂は成形性が悪く、生産性およびコ
ストの面で工業用としては不適当である。Among the performances required of this CFRP, heat resistance, chemical resistance, etc. are largely influenced by the type of matrices and resins. For example, epoxy resins that have good adhesion to carbon fibers may have insufficient heat resistance. On the other hand, polyimide resins which have excellent heat resistance have poor moldability and are unsuitable for industrial use in terms of productivity and cost.
PPS樹脂は卓越し念耐熱性、耐薬品性および剛性を有
する高性能熱可塑性樹脂として注目されているが、この
樹脂は未架橋のpps樹脂を炭素繊維に含浸し念後の熱
処理時にPPSの架橋反応に伴って発生するラジカルが
炭素値維を劣化させること、また、その伸びが小さい之
めに成形後のCFRPはサーマルクラックが発生し易く
、強度あるいは眉間剪断強度〔以下ILSSと略す〕が
低いこと、および上記架橋化のための熱処理に#う成形
時間の延長が生産性を低下させることなどの理由で、C
FRP用のマ) IJフックス脂として未だ実用化され
るに到っていない。PPS resin is attracting attention as a high-performance thermoplastic resin with excellent heat resistance, chemical resistance, and rigidity, but this resin impregnates carbon fiber with uncrosslinked PPS resin and cross-links the PPS during post-heat treatment. The radicals generated during the reaction deteriorate the carbon fiber, and because the elongation is small, thermal cracks are likely to occur in CFRP after molding, and the strength or glabella shear strength (hereinafter abbreviated as ILSS) is low. In addition, the heat treatment for crosslinking mentioned above increases the molding time, which reduces productivity.
It has not yet been put into practical use as IJ Fuchs resin for FRP.
一方、上記の欠点を改良する念めにマトリックス樹脂と
して特定範囲量のポリサルホンを混合したpps樹脂組
成物を用いる方法が%開昭55−82130号に開示さ
れているが、PPSとポリサルホンとの相溶性が不十分
なために、 ppsの可撓性あるいは機械的強度が十分
に改良されず、必ずしも満足すべきCFRPを供給する
に到っていない。On the other hand, in order to improve the above-mentioned drawbacks, a method using a pps resin composition mixed with polysulfone in a specific range as a matrix resin is disclosed in Japanese Patent Publication No. 82130/1982, but the interaction between PPS and polysulfone is Due to insufficient solubility, the flexibility or mechanical strength of pps cannot be sufficiently improved, and it is not always possible to provide a satisfactory CFRP.
(問題点を解決する九めの手段〕
本発明者らは、PPSの長所を備えその欠点である可撓
性が改良され、炭素繊維の劣化、CFRPのサーマルク
ラック等が実質的に発生しない樹脂組成物を得るべく鋭
意検討した結果、末端反応性基をもつppsとppss
の共重合反応により両者を化学的に結合させてなる樹脂
をマトリックス樹脂として用いることが有効であること
を見出し、本発明に到達したものである。(Ninth Means for Solving the Problems) The present inventors have developed a resin that has the advantages of PPS, improves its disadvantage of flexibility, and substantially eliminates deterioration of carbon fibers, thermal cracks of CFRP, etc. As a result of intensive studies to obtain compositions, we found that pps and ppss, which have terminal reactive groups.
The inventors have discovered that it is effective to use as a matrix resin a resin formed by chemically bonding the two through a copolymerization reaction, and have thus arrived at the present invention.
即ち、本発明はPPSとppssから成るブロック共重
合体を必須成分として含む樹脂組成物を炭素繊維に含浸
してなる耐熱性、耐薬品性ならびに可撓性等の機械的性
質に優れたCFRPを提供するものである。That is, the present invention uses CFRP, which has excellent mechanical properties such as heat resistance, chemical resistance, and flexibility, and is made by impregnating carbon fibers with a resin composition containing as an essential component a block copolymer composed of PPS and ppss. This is what we provide.
本発明におけるプロ、り共重合体の成分および該共重合
体と混合され得るPPSは一般式上含むものが特性の優
れた組成物をもたらすことから好ましい。ま几、かかる
PPSはその対数粘度〔η〕(ここで、〔η〕は0.4
.9/Zooゴのm液なる?リマー濃度において、α−
クロルナフタレン中206℃で測定し、下式
〔η)=An(相対粘度)/?テリー濃度て従い算出し
た値である。〕が0.03〜0.80の範囲のものが好
ましい。In the present invention, components of the pro-copolymer and PPS that can be mixed with the copolymer are preferably those included in the general formula because they provide a composition with excellent properties. However, such PPS has a logarithmic viscosity [η] (where [η] is 0.4
.. 9/Zoo Go's m liquid? At the reamer concentration, α-
Measured in chlornaphthalene at 206°C, using the following formula [η) = An (relative viscosity)/? This is the value calculated according to the terry concentration. ] is preferably in the range of 0.03 to 0.80.
このテリマーの重合方法としては、ハロダン置換芳香族
化合物、例えばp−ジクロルベンゼンを硫黄と炭酸ソー
ダの存在下で重合させる方法、極性溶媒中で硫化ナトリ
ウムあるいは水硫化ナトリウムと水酸化ナトリウム又は
硫化水素と水酸化ナトリウムあるいはナトリウムアミノ
アルカノエートの存在下で重合させる方法、p−クロル
チオフェノールの自己縮合などがあげられるが、N−メ
チルピロリドン、ジメチルアセトアミドなどのアミド系
溶媒やスルホラン等のスルホン系醇媒中で硫化ナトリウ
ムとp−ジクロルベンゼンを反応させる方法が適当であ
る。この際に重合度を調節するためにカルメン酸やスル
ホン酸、またはリン酸のアルカリ金属塩を添加したり、
水酸化アルカリを添加することは好ましい方法である。Polymerization methods for this tellimer include a method in which a halodane-substituted aromatic compound, such as p-dichlorobenzene, is polymerized in the presence of sulfur and sodium carbonate, and a method in which a halodane-substituted aromatic compound, such as p-dichlorobenzene, is polymerized in the presence of sulfur and sodium carbonate; Examples include polymerization in the presence of sodium hydroxide or sodium aminoalkanoate, and self-condensation of p-chlorothiophenol. A suitable method is to react sodium sulfide and p-dichlorobenzene in a medium. At this time, to adjust the degree of polymerization, carmenic acid, sulfonic acid, or an alkali metal salt of phosphoric acid may be added.
Adding alkali hydroxide is a preferred method.
共重合成分として、30モル幅未満であれば、メタ結合
基、フェニル基、アルコキシ基、カルノン酸基ま九はカ
ルメン酸の金属塩基を示す)、3官能結合の結晶性に大
きく影響しない範囲でかまわないが、好ましくは共重合
成分は10モル係以下がよい。As copolymerization components, if the molar width is less than 30, meta-bonding groups, phenyl groups, alkoxy groups, carnoic acid groups (indicates metal bases of carmenic acid), within a range that does not significantly affect the crystallinity of the trifunctional bond. However, preferably the copolymerization component is 10 molar or less.
特に3官能性以上のフェニル、ビフェニル、ナフチルス
ルフィド結合などを共重合に選ぶ場合は3モル係以下が
よい。In particular, when a trifunctional or more functional phenyl, biphenyl, naphthyl sulfide bond, etc. is selected for copolymerization, the molar ratio is preferably 3 or less.
かかるPPSの具体的な製造法としては、例えば(1)
ハロダン置換芳香族化合物と硫化アルカリとKよる製法
(米国特許第2513188号、特公昭44−2767
1号、特公昭45−3368号および特公昭52−12
240号参照)、(2)チオフェノール類のアルカリ触
媒又は銅塩等の共存下における縮合反応による製法(米
国特許第3274165号および英国特許第11606
60号参照)、(3)芳香族化合物を塩化硫黄とのルイ
ス竣触媒共存下に於ける縮合反応による製法(特公昭4
6−27255号およびベルギー特許第29437号参
照〕等が挙げられる。As a specific method for producing such PPS, for example, (1)
Production method using halodane-substituted aromatic compound, alkali sulfide and K (US Pat. No. 2,513,188, Japanese Patent Publication No. 44-2767)
1, Special Publication No. 45-3368 and Special Publication No. 52-12
240), (2) A method for producing thiophenols by condensation reaction in the presence of an alkali catalyst or copper salt (US Pat. No. 3,274,165 and British Pat. No. 11,606)
(Refer to No. 60), (3) Production method by condensation reaction of an aromatic compound with sulfur chloride in the coexistence of a Lewis catalyst (Special Publication No. 4)
6-27255 and Belgian Patent No. 29437].
本発明におけるブロック共重合体は、例えばpps s
の末端基とPPSの末端基とを反応せしめることによっ
て得られるため、例えばppssの末端基が場合、PP
Sの末端基をナトリウムスルフィド基(構造式: Na
5− )の如き反応性基にしておく必要がある。かかる
pps 1得る方法として、予め重合反応時にモノマー
の硫化ナトリウム成分の量をp−ジクロルベンゼン成分
に対し1〜20モル憾過剰の状態で反応させる方法が挙
げられる。The block copolymer in the present invention is, for example, pps s
It is obtained by reacting the terminal group of ppss with the terminal group of PPS, so for example, if the terminal group of ppss is
The terminal group of S is a sodium sulfide group (structural formula: Na
It is necessary to use a reactive group such as 5-). An example of a method for obtaining such pps 1 is to react the sodium sulfide component of the monomer in advance in a 1 to 20 molar excess with respect to the p-dichlorobenzene component during the polymerization reaction.
一方、本発明のブロック共重合体を構成するするポリマ
ーとして定義される。このポリマーの分子漬は対数粘度
η1nh(ここで、ηinhは0.5/100ゴの溶液
なる?リマー濃度においてフェノール/1.1,2.2
−テトラクロルエタン(3:2重量比)混合溶媒中30
℃で測定し、下式
η1nh=tn(相対粘度)/ポリマー濃度に従い算出
し元値である。〕がO,OS〜1.0の範囲のものが好
ましい。このポリマーの重合方法としては、例えばジハ
ロ芳香族スルホンとアルカリ金属硫化物を有機アミド浴
媒中で反応させる方法(米国特許第4102875号参
照)が挙げられる。On the other hand, it is defined as a polymer constituting the block copolymer of the present invention. The molecular solution of this polymer has a logarithmic viscosity η1nh (where ηinh is a solution of 0.5/100 phenol/1.1, 2.2
-30% in tetrachloroethane (3:2 weight ratio) mixed solvent
The original value is calculated according to the following formula: η1nh=tn (relative viscosity)/polymer concentration. ] is preferably in the range of O, OS to 1.0. Examples of polymerization methods for this polymer include a method in which a dihaloaromatic sulfone and an alkali metal sulfide are reacted in an organic amide bath medium (see US Pat. No. 4,102,875).
本発明のブロック共重合体を合成する際に用いを有する
ものであり、これを得る方法としては、ポリマー合成反
応時にジノ・口芳香族スルホンの量をアルカリ金属硫化
物の量に対し、例えば5モル係過剰の状態で反応させる
方法(米国特許第4301274号参照)が挙げられる
。It is useful when synthesizing the block copolymer of the present invention, and the method for obtaining it is such that, during the polymer synthesis reaction, the amount of Dino-Kuchi aromatic sulfone is, for example, 5% relative to the amount of alkali metal sulfide. A method of reacting in a molar excess state (see US Pat. No. 4,301,274) can be mentioned.
本発明の方法においてppssとPPSの共重合反応を
行なう際、第3成分としてジハロ芳香族スルホンあるい
は硫化ナトリウム等の結合剤を添加する方法を用いるこ
ともさしつかえない。ま九、ブロック共重合体である本
発明の目的を逸脱しない範囲で、PPSとppssのい
ずれか一方のポリマーの存在下に他方のモノマー成分を
重合し、最終的に共重合体を得る方法を用いることもで
きる。When performing the copolymerization reaction of ppss and PPS in the method of the present invention, it is also possible to use a method of adding a binder such as dihaloaromatic sulfone or sodium sulfide as a third component. Ninth, without departing from the purpose of the present invention, which is a block copolymer, there is a method of polymerizing either PPS or ppss in the presence of the other monomer component to finally obtain a copolymer. It can also be used.
ま之、共重合反応する際、PPSとppssの末端反応
性基の数を同じにすることは、収率よくブロック共重合
体が得られ最も好ましい。一方、いずれか一方の成分の
末端基数が過剰の場合、反応終了後、未反応のホモ?リ
マー成分のみを分別あるいは抽出除去すること知よって
ブロック共重合体のみ全回収することができる。However, when carrying out the copolymerization reaction, it is most preferable to make the number of terminal reactive groups of PPS and ppss the same, since a block copolymer can be obtained in good yield. On the other hand, if the number of terminal groups of either component is excessive, after the reaction is completed, unreacted homozygotes remain? By separating or extracting only the remer component, only the block copolymer can be completely recovered.
共重合反応において使用される溶媒は、その温度および
圧力において実質的に液状である有機極性溶媒が好まし
い。具体的には、ホルムアミド、アセトアミド、N−メ
チルホルムアミド、N、N−ジメチルホルムアミド、N
、N−ツメチルアセトアミド、2−ピロリドン、N−メ
チル−2−ピロリドン、N−エチル−2−ピロリドン、
!−カグロラクタム、N−メチルーε−カプロラクタム
、ヘキサメチルホスホルアミド、テトラメチル尿素、1
.3−ジメチル−2−イミダゾリ・ジノン等のアミド、
尿素およびラクタム類;スルホラン、ジメチルスルホラ
ン等のスルホン類;ベンゾニトリル等のニトリル類;メ
チルフェニルケトン等のケトン類等およびこれらの混合
物を挙げることができる。The solvent used in the copolymerization reaction is preferably an organic polar solvent that is substantially liquid at that temperature and pressure. Specifically, formamide, acetamide, N-methylformamide, N,N-dimethylformamide, N
, N-trimethylacetamide, 2-pyrrolidone, N-methyl-2-pyrrolidone, N-ethyl-2-pyrrolidone,
! -caglolactam, N-methyl-ε-caprolactam, hexamethylphosphoramide, tetramethylurea, 1
.. Amides such as 3-dimethyl-2-imidazolidinone,
Examples include urea and lactams; sulfones such as sulfolane and dimethylsulfolane; nitriles such as benzonitrile; ketones such as methylphenyl ketone; and mixtures thereof.
これらの溶媒のうちでは、アミド類、ラクタム類あるい
はスルホン類等の非プロトン性有機極性溶媒を使用する
ことが特に好ましい。有機極性溶媒の使用量は、j?’
lJマー成分の量て対する重量比で2〜20の範囲で、
好ましくは3〜1oの範囲である。Among these solvents, it is particularly preferable to use aprotic organic polar solvents such as amides, lactams, or sulfones. The amount of organic polar solvent used is j? '
The weight ratio to the amount of lJmer component is in the range of 2 to 20,
Preferably it is in the range of 3 to 1o.
ブロック化反応による共重合反応’t=成吻が化学的に
結合しeppsとppssとのブロック共重合体である
ことは、得られ九ポリマーをppssの良溶媒であるフ
ェノール/テトラクロルエタン(3:2重量比〕混合溶
媒でくり返し抽出した後、抽出液中にppssがもはや
含まれないにもかかわらず、ポリマー中にこの成分が存
在していることで確かめられる。一方、共重合反応生成
物中に未反応のPPSが含まれるかどうかは、その生成
物をPPSの良溶媒であるα−クロルナフタレンを用い
分別沈濃を行ない、PPSホモポリマーが存在するか否
かで確認できる。Copolymerization reaction by block reaction 't=nose is chemically bonded to form a block copolymer of epps and ppss. :2 weight ratio] Even though ppss is no longer contained in the extract after repeated extraction with a mixed solvent, the presence of this component in the polymer is confirmed.On the other hand, the copolymerization reaction product Whether or not unreacted PPS is contained in the product can be confirmed by performing fractional precipitation of the product using α-chlornaphthalene, which is a good solvent for PPS, and checking whether PPS homopolymer is present.
ま念、共重合反応する際、ppsとppssとの割合は
目的とする特性によって異なるが、ppss成分とPP
S成分との重量比が一般的には1〜99/99〜1、好
ましくは5〜90/95〜10の範囲である。上記重量
比が1799未満であればppssによって付与される
可撓性等の効果が発現できず、ま九、99/1を越える
と本特許の目的とする効果が得られず好ましくない。Please note that when performing a copolymerization reaction, the ratio of pps and ppss varies depending on the desired properties, but the ppss component and PP
The weight ratio with the S component is generally in the range of 1 to 99/99 to 1, preferably 5 to 90/95 to 10. If the weight ratio is less than 1799, the effects such as flexibility imparted by ppss cannot be achieved, and if it exceeds 99/1, the effects aimed at in this patent cannot be obtained, which is not preferable.
尚、本発明で用いられるブロック共重合体は対数粘度〔
η〕(ここで、〔η〕は0.4 N/100ゴの溶液な
るポリマー濃度においてα−クロルナフタレン中206
℃で測定し、下式
〔η)=Afl(相対粘度〕/−リマー濃度に従い算出
した値である。〕が0.03〜1.0の範囲であるもの
が好ましい。The block copolymer used in the present invention has a logarithmic viscosity [
η] (where [η] is 206 in α-chlornaphthalene at a polymer concentration of 0.4 N/100g solution)
It is a value calculated according to the following formula [η)=Afl(relative viscosity]/−limer concentration] in the range of 0.03 to 1.0 when measured at ℃.
本発明の樹脂組成物は、前記ブロック共重合体3〜10
.0重量部、より好ましくは10〜100重量部に対し
てPPSを併用する場合にはPPSを好ましくは1〜9
7重量部、より好ましくは10〜90重量部、ppss
を併用する場合にはppssを好ましくは1〜60重量
部、より好ましくは10〜40重量部含有するものであ
る。尚、本発明の樹脂組成物は該プロ、り共1合体t−
3〜100重量部分含むことにより可撓性の改善効果が
大きく、CFRPのサーマルクラ、り等が発生し難いの
で好ましいO
又、本発明の樹脂組成物は前記ブロック共重合体を製造
する際にPPS成分i&はppss成分のいずれか一方
を過剰量にして反応せしめることによシ得ることができ
る。その際、遊離のPPSおよびppssが含有されて
いることは、ppssの良溶媒であるN−メチルピロリ
ドンやフェノール/テトラクロルエタン混合溶媒でくり
返し抽出し九後のポリマー中に一定量のppssが含ま
れていることで確かめられ、一方、PPSホモポリマー
が混在しているかどうかはα−クロルナフタレンを用い
る分別沈澱実験によって確かめることができる。The resin composition of the present invention comprises the block copolymers 3 to 10
.. When PPS is used in combination with 0 parts by weight, more preferably 10 to 100 parts by weight, PPS is preferably 1 to 9 parts by weight.
7 parts by weight, more preferably 10 to 90 parts by weight, ppss
When used together, ppss is preferably contained in an amount of 1 to 60 parts by weight, more preferably 10 to 40 parts by weight. Incidentally, the resin composition of the present invention is a monomer t-
It is preferable that the resin composition of the present invention contains 3 to 100 parts by weight because it has a great effect of improving flexibility and is less likely to cause thermal cracking, cracking, etc. of CFRP. The PPS component i& can be obtained by reacting one of the ppss components in excess. At that time, the presence of free PPS and ppss means that a certain amount of ppss is contained in the polymer after repeated extraction with N-methylpyrrolidone or a mixed solvent of phenol/tetrachloroethane, which is a good solvent for ppss. On the other hand, whether or not PPS homopolymer is present can be confirmed by a fractional precipitation experiment using α-chlornaphthalene.
本発明に使用する炭素繊維は比較的長繊維、通常長さが
7日以上、好ましくは1の以上のものであり、レーヨン
系、Iリアクリルニトリル系、ピッチ系などいかなる種
類のものでもよいし、炭素繊維の形態もヤーン、ロービ
ング、カットファイバー、織物、編物、組物などいずれ
の形態でもさしつかえない。The carbon fibers used in the present invention are relatively long fibers, usually having a length of 7 days or more, preferably 1 or more days, and may be of any type such as rayon type, I-lyacrylonitrile type, or pitch type. The carbon fiber may be in any form such as yarn, roving, cut fiber, woven fabric, knitted fabric, or braided fabric.
tfc、本発明の樹脂組成物には、本発明の目的を逸脱
しない範囲で熱可塑性樹脂、エポキシ樹脂等の他種ポリ
マー、あるいは添加剤、充填剤が配合されていてもさし
つかえない。さらに、強化用繊維としてガラス繊維、お
よびアラミド繊維や芳香族ポリエステル繊維等の有機繊
維等の他の強化用繊維が併用されていてもさしつかえな
い。TFC, the resin composition of the present invention may contain other types of polymers such as thermoplastic resins and epoxy resins, additives, and fillers without departing from the purpose of the present invention. Furthermore, as reinforcing fibers, other reinforcing fibers such as glass fibers and organic fibers such as aramid fibers and aromatic polyester fibers may be used in combination.
本発明の樹脂組成物は、樹脂成分と炭素繊維とを通常固
形分重量比で20/80〜80/20、好ましくは30
/70〜60/40となるように含有される。In the resin composition of the present invention, the solid content weight ratio of the resin component and carbon fiber is usually 20/80 to 80/20, preferably 30/80 to 80/20.
/70 to 60/40.
本発明の樹脂組成物を炭素繊維に含浸する手段としては
特に限定されるものではなく、各種の方法がある。例え
ば樹脂粉末、スラリー、あるいは樹脂溶液等をスプレー
を用いて含浸させる方法などが挙げられる。さらK、本
発明の樹脂組成物を好ましくは300〜360℃に加熱
して溶融し、これを炭素繊維に段階的もしくは連続的に
含浸、成形してもよい。加熱方法として樹脂を増感剤存
在下で高周波加熱する方法等がある。成形は通常300
〜360℃で少なくとも100に!g/α8の加圧下に
行ない、ついで除冷もしくは急冷することができる。The means for impregnating carbon fibers with the resin composition of the present invention is not particularly limited, and there are various methods. For example, a method of impregnating resin powder, slurry, resin solution, etc. using a spray can be mentioned. Furthermore, the resin composition of the present invention may be melted by heating preferably to 300 to 360° C., and carbon fibers may be impregnated with this in stages or continuously and molded. As a heating method, there is a method of high-frequency heating of the resin in the presence of a sensitizer. Molding is usually 300
~360℃ to at least 100! It can be carried out under a pressure of g/α8, and then slowly or rapidly cooled.
(発明の効果)
本発明の特徴は炭素繊維て含浸すべきマトリックス樹脂
として、PPSおよびこれと相溶性の悪いppssとの
単なるブレンドによって得られる樹脂と異なり、両成分
のポリマー鎖が化学的に結合したプロ、り共重合体を含
む樹脂を用いる点にある。(Effects of the Invention) The feature of the present invention is that, unlike resins obtained by simply blending PPS and ppss, which have poor compatibility, the polymer chains of both components are chemically bonded as a matrix resin to be impregnated with carbon fibers. The point is that a resin containing a polypropylene copolymer is used.
即ち、PPSの耐熱性、耐薬品性が保持され、かつ可撓
性が改良され九マトリックス樹脂を用いることによって
CFRPのサーマルクラックの発生が抑制され、まe
ppsの加熱架橋工程時の炭素繊維の劣化Cて伴なう強
度あるいはILSSの低下が防止される。In other words, the heat resistance and chemical resistance of PPS are maintained, the flexibility is improved, and the occurrence of thermal cracks in CFRP is suppressed by using the matrix resin.
Decrease in strength or ILSS caused by deterioration C of carbon fibers during the thermal crosslinking process of pps is prevented.
従って、本発明のCFRPはPPS !/C起因する炭
素繊維の劣化、サーマルクラックがなく、しかもPPS
の優れ念耐熱性、耐薬品性、炭素繊維に対する接着性が
具備された高性能CFRPであり、航空・宇宙用途等に
適用することができる。Therefore, the CFRP of the present invention is PPS! /C-induced carbon fiber deterioration and thermal cracking, and PPS
It is a high-performance CFRP with excellent heat resistance, chemical resistance, and adhesion to carbon fibers, and can be applied to aerospace and other applications.
(実施例〕
以下、本発明を実施例によジ具体的に説明するが、本発
明はこれらに限定されるものではない。(Examples) Hereinafter, the present invention will be specifically explained with reference to Examples, but the present invention is not limited thereto.
実施例1.比較例1および2
まず、107オートクレープにN−メチルピロリドン1
980I!、硫化ナトリウム2.7水塩65511(5
,0モル〕、水酸化ナトリウム2.0.F、およびビス
(p−クロルフェニル)スルホン1436、p(s、o
モル〕を仕込み、窒素雰囲気下、200℃まで昇温しそ
の温度で攪拌下6時間反応させ念。Example 1. Comparative Examples 1 and 2 First, N-methylpyrrolidone 1 was placed in a 107 autoclave.
980I! , sodium sulfide hemihydrate 65511 (5
,0 mol], sodium hydroxide 2.0. F, and bis(p-chlorophenyl)sulfone 1436, p(s, o
mol], heated to 200°C under a nitrogen atmosphere, and allowed to react at that temperature for 6 hours with stirring.
次いでこの系にビス(p−クロルフェニル)スルホン7
2g(0,25モル)t−N−メチルピロリドン200
gK溶かした液を添加し、さらに1時間反応させた。反
応容器を冷却後、内容物を取出し、熱水とアセトンで数
回洗浄し、ポリマーケーキを戸別した。このケーキを8
0〜150℃で減圧乾燥し、淡褐色のポリマー119O
Nを得t(収率96チ)。このポリマーの対数粘度η1
nh(ここで、ηinhは0.5y100 rntの溶
液なるポリマー濃度においてフェノール/ 1,1,2
.2−テトラクロルエタン(3:2重量比〕混合溶媒中
30℃で測定し、下式
η1nh=tn(相対粘度)/ポリマー濃度に従い算出
した値である。〕は0.22であり7t。Next, bis(p-chlorophenyl)sulfone 7 was added to this system.
2g (0.25 mol) t-N-methylpyrrolidone 200
A solution containing gK was added and the reaction was further continued for 1 hour. After the reaction vessel was cooled, the contents were taken out, washed several times with hot water and acetone, and the polymer cake was sent door to door. 8 pieces of this cake
Dry under reduced pressure at 0 to 150°C to obtain light brown polymer 119O.
N was obtained (yield: 96 cm). Logarithmic viscosity η1 of this polymer
nh (where ηinh is phenol/1,1,2 at a polymer concentration of 0.5y100 rnt solution)
.. The value was measured in a mixed solvent of 2-tetrachloroethane (3:2 weight ratio) at 30°C and calculated according to the following formula η1nh=tn (relative viscosity)/polymer concentration.] is 0.22, which is 7t.
引続き、101オートクレーグにN−メチルピロリドン
3100#と硫化ナトリウム2.7水塩1009 F
(7,7モル)および水酸化ナトリウム3.5.9 (
0,09モル〕を仕込み、窒素雰囲気下、200℃まで
約2時間かけて攪拌しながら昇温して2201dの水を
留出させt0反応系を150℃に冷却した後、p−ジク
ロルベンゼン102911(7,0モル〕、N−メチル
ピロリドン700Iを加え、230℃で1.5時間、次
いで260℃で2時間反応させた。重合終了時の内圧は
7.0kg/iであり念。反応容器を冷却後、内容物の
一部をサンプリングし戸別した後、ケーΦを熱水で3回
煮沸洗浄し、さらにアセトンで2回洗浄し念後、120
℃で乾燥して淡灰褐色粉末状pps 、x リマーを得
た(収率約94係)。このポリマーの対数粘度〔η〕(
ここで、〔η〕はポリマー濃度0.4 、F/100d
、α−クロルナフタレン中206℃で測定し、〔η)=
tn(相対粘度)/ポリマー濃度に従い算出し比値であ
る〕は0.14であった。Subsequently, add N-methylpyrrolidone 3100 # and sodium sulfide 2.7 hydrate to 101 autoclave 1009 F.
(7.7 mol) and sodium hydroxide 3.5.9 (
0.09 mol] was charged, the temperature was raised to 200°C under nitrogen atmosphere with stirring for about 2 hours, water of 2201d was distilled out, and the t0 reaction system was cooled to 150°C, and then p-dichlorobenzene was added. 102911 (7.0 mol) and N-methylpyrrolidone 700I were added and reacted at 230°C for 1.5 hours and then at 260°C for 2 hours.The internal pressure at the end of the polymerization was 7.0 kg/i. After cooling the container, a portion of the contents was sampled and distributed from house to house, and the case Φ was boiled and washed three times with hot water, and then twice with acetone.
It was dried at 0.degree. C. to obtain a light grayish brown powder of pps,x remer (yield: about 94%). Logarithmic viscosity of this polymer [η] (
Here, [η] is polymer concentration 0.4, F/100d
, measured in α-chlornaphthalene at 206°C, [η)=
The ratio value calculated according to tn (relative viscosity)/polymer concentration was 0.14.
次いで、上記のPPS重合重合金混合物2370g述の
末端クロルフェニル基型PPSS3QOgおよびN−メ
チルピロリドン1200#を加え、窒素・4−ノ後密封
し220℃まで昇温し、この温度で3時間反応させ九。Next, 2370 g of the above-mentioned PPS polymerized polymer mixture, the terminal chlorphenyl group type PPSS3QOg and 1200 # of N-methylpyrrolidone were added, and after nitrogen gas, the mixture was sealed, heated to 220°C, and reacted at this temperature for 3 hours. Nine.
反応容器を冷却後、内容物をテ別し、固形分をN−メチ
ルピロリドンで2回洗浄し念後、熱水で3回煮沸洗浄し
t0得られ九ケーキを120℃で5時間乾燥して486
Iの淡褐色粉末状ポリマーを得九。このポリマー〔η〕
は0.19であった。After cooling the reaction vessel, the contents were separated by sieve, the solid content was washed twice with N-methylpyrrolidone, and then boiled and washed three times with hot water.The nine cakes obtained were dried at 120°C for 5 hours. 486
A light brown powdery polymer of I was obtained. This polymer [η]
was 0.19.
tた、このポリマーの赤外線吸収スにクトルを測定し九
ところ、ppsとppssの吸収以外のピークは観察さ
れず、かつ1320(7FI 、620帰 および48
0 cm−1に見られる特性吸収の強度からppssを
定量し九ところ、ポリマー中に46.0重i%含゛まれ
ていた。同時に、ポリマーの元素分析を行ない:イオウ
含量を定量し念ところ、27.87 %の値を示し、ポ
リマー中にppssが46.0重を壬含まれていること
を確認し念。In addition, when we measured the infrared absorption coefficient of this polymer, no peaks other than pps and ppss absorption were observed, and 1320 (7FI, 620 return and 48
The ppss was determined from the intensity of the characteristic absorption observed at 0 cm-1, and was found to be 46.0% by weight in the polymer. At the same time, elemental analysis of the polymer was carried out: the sulfur content was quantified and showed a value of 27.87%, confirming that the polymer contained 46.0 parts by weight of ppss.
さらに、上記ポリマーの溶媒抽出実験を行なった。即ち
、ppssの良溶媒であるN−メチルピロリドンに上記
ポリマーを分散させ、100℃で未反応のpps sを
抽出除去することを試みた。しかし、ppssは全く溶
出せず、かつ抽出実験後回収した上記、41Jマーの赤
外線吸収スペクトルの測定よりppssの含量は46.
0重量俤でありtoこれらの結果から、本実施例の共重
合反応生成物がPPSとppssが化学的に結合し念!
ロック共重合体であることを確認し念。Furthermore, a solvent extraction experiment of the above polymer was conducted. That is, an attempt was made to disperse the above polymer in N-methylpyrrolidone, which is a good solvent for ppss, and extract and remove unreacted ppss at 100°C. However, ppss was not eluted at all, and the infrared absorption spectrum measurement of the 41J mer recovered after the extraction experiment revealed that the ppss content was 46.
From these results, we can confirm that PPS and ppss are chemically bonded in the copolymerization reaction product of this example!
Be sure to confirm that it is a lock copolymer.
次いで、このポリマーをクロロホルムに分散すせて雪脂
溶液を調整し食後、これを東しく株)j!!!の炭素繊
維トレカT−300を用い縦/横=1/1の炭素繊維ク
ロスに含浸させ、さらにクロロホルムを乾燥除去してグ
リプレグを作成し念。このグリプレグを積層して金型に
入れ、350℃で40分加熱架橋させた後、120〜4
20−7cm”の範囲で加圧しt後冷却し、金型が14
0℃まで冷却しt時点で成形品を取出した。なお、成形
品の炭素涜維含有量は60重量憾に調節した。成形品を
150℃で1.5時間アニーリングを行なう7を後、A
STMD−2344々らびにASTMD −790に準
じて曲げ強度ならびにILSSを測定し念。結果を表−
1に示した。Next, this polymer was dispersed in chloroform to prepare a snow fat solution, and after a meal, this was poured into Toshiku Co., Ltd.)j! ! ! Using carbon fiber Trading Card T-300, a carbon fiber cloth with length/width ratio of 1/1 was impregnated, and chloroform was further removed by drying to create Gripreg. This Gripreg was laminated and put into a mold, and after heating and crosslinking at 350℃ for 40 minutes,
Pressure is applied in the range of 20-7 cm” and then cooled, and the mold becomes 14 cm.
The molded product was cooled to 0° C. and taken out at time t. The carbon fiber content of the molded product was adjusted to 60% by weight. After step 7 of annealing the molded product at 150°C for 1.5 hours, A
Bending strength and ILSS were measured in accordance with STMD-2344 and ASTM D-790. Display the results -
Shown in 1.
比較例1では、実施例1で得e ppss粉末と、pp
s重合生成物を通常処理して得たPPS粉末をポリマー
中ppssが46.0を看慢含む混合物を用い、実施例
1と同様にして、成形品を得た。ま念、比較例2では、
上記のPPS粉末のみを含浸させ、同様だして成形品を
取出し念。表−1に結果を示したように、ppss無添
加の場合あるいはPPSとppssの混合物を用い念場
合に比べ、PPS/PP5Sのブロック共重合体を含む
ポリマーを用いて得た成形品は、曲げ強度およびILS
Sがいずれも大きく、物性が良好であう念。In Comparative Example 1, the e ppss powder obtained in Example 1 and the ppss powder obtained in Example 1 were used.
A molded article was obtained in the same manner as in Example 1 using a mixture containing PPS powder obtained by conventional treatment of the polymerization product with a ppss of 46.0 in the polymer. Seriously, in Comparative Example 2,
Impregnate only the above PPS powder and take out the molded product in the same manner. As shown in Table 1, the molded product obtained using the polymer containing the PPS/PP5S block copolymer was more bendable than the case without the addition of ppss or when a mixture of PPS and ppss was used. Strength and ILS
S is large in all cases, and the physical properties are good.
表−1
実施例2
実施例1と同様にして、ポリマー混合物中ppssを1
8.0重+i幅含むppsとPPS /PP5Sのブロ
ック共重合体の混合物(PPS /ブロック共重合体の
重量化=15/85)を合成し友。このポリマーの〔η
〕は0,18であり念。予め実施例1で合成したpps
sホモ?リマーを樹脂成分中5.0重量係合まれるよう
にクロロホルムて溶かし之溶液て、前記の共重合体混合
物を分散させ、全体として樹脂成分中ppssが23.
0重量係の樹脂溶液を調整し念。以下、加熱架橋時間を
30分にした以外は実施例1と同様にして成lk取出し
、物性1価したところ、23℃および150℃での曲げ
強度はそれぞれ77 kg/rrm” オ上U 38
kg/m” ト’4VCK ’IN テノ物性が良好で
あり、また、23℃でのILSSも6,7Kg /ms
”と良好であった。Table 1 Example 2 In the same manner as in Example 1, ppss was added to 1 in the polymer mixture.
A mixture of pps containing 8.0 weight + i width and a block copolymer of PPS/PP5S (weight of PPS/block copolymer = 15/85) was synthesized. This polymer [η
] is 0.18, just in case. pps synthesized in advance in Example 1
s homo? The above copolymer mixture was dispersed by dissolving the reamer in chloroform so that 5.0% by weight of the reamer was incorporated in the resin component, and the total ppss in the resin component was 23.0% by weight.
Make sure to adjust the resin solution for 0 weight. The following procedure was repeated in the same manner as in Example 1 except that the heating crosslinking time was changed to 30 minutes, and when the physical properties were evaluated, the bending strength at 23°C and 150°C was 77 kg/rrm, respectively.
kg/m” to'4VCK'IN Good physical properties, and ILSS at 23℃ is 6.7Kg/ms
“It was good.
Claims (1)
スルホンとが化学的に結合したブロック共重合体と、ポ
リフェニレンスルフィドおよびポリフェニレンスルフィ
ドスルホンの少なくとも一種との混合物を炭素繊維に含
浸してなる炭素繊維強化樹脂組成物。A carbon fiber reinforced resin composition obtained by impregnating carbon fibers with a mixture of a block copolymer in which polyphenylene sulfide and polyphenylene sulfide sulfone are chemically bonded, and at least one of polyphenylene sulfide and polyphenylene sulfide sulfone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26989586A JPH0745574B2 (en) | 1986-11-14 | 1986-11-14 | Carbon fiber reinforced resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26989586A JPH0745574B2 (en) | 1986-11-14 | 1986-11-14 | Carbon fiber reinforced resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63125531A true JPS63125531A (en) | 1988-05-28 |
JPH0745574B2 JPH0745574B2 (en) | 1995-05-17 |
Family
ID=17478713
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP26989586A Expired - Fee Related JPH0745574B2 (en) | 1986-11-14 | 1986-11-14 | Carbon fiber reinforced resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0745574B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0388970A2 (en) * | 1989-03-23 | 1990-09-26 | Phillips Petroleum Company | Thermoplastic resin compositions and methods |
EP0388969A2 (en) * | 1989-03-23 | 1990-09-26 | Phillips Petroleum Company | Composites having reduced microcracking and methods of making the same |
JPH0598042A (en) * | 1991-10-03 | 1993-04-20 | Toray Ind Inc | Fibrous sheet impregnated with polyphenylene sulfide resin |
CN110591095A (en) * | 2019-09-10 | 2019-12-20 | 珠海长先新材料科技股份有限公司 | Synthetic method of polyphenylene sulfide and polysulfone thioether block polymer |
WO2020196109A1 (en) | 2019-03-26 | 2020-10-01 | 東レ株式会社 | Fiber-reinforced resin base material |
CN112876734A (en) * | 2021-01-13 | 2021-06-01 | 西北工业大学 | Method for recycling epoxy resin-based carbon fiber composite material under mild condition |
CN116396092A (en) * | 2023-04-07 | 2023-07-07 | 湖南远辉复合材料有限公司 | Preparation method of C/C composite material |
-
1986
- 1986-11-14 JP JP26989586A patent/JPH0745574B2/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0388970A2 (en) * | 1989-03-23 | 1990-09-26 | Phillips Petroleum Company | Thermoplastic resin compositions and methods |
EP0388969A2 (en) * | 1989-03-23 | 1990-09-26 | Phillips Petroleum Company | Composites having reduced microcracking and methods of making the same |
JPH0598042A (en) * | 1991-10-03 | 1993-04-20 | Toray Ind Inc | Fibrous sheet impregnated with polyphenylene sulfide resin |
WO2020196109A1 (en) | 2019-03-26 | 2020-10-01 | 東レ株式会社 | Fiber-reinforced resin base material |
CN110591095A (en) * | 2019-09-10 | 2019-12-20 | 珠海长先新材料科技股份有限公司 | Synthetic method of polyphenylene sulfide and polysulfone thioether block polymer |
CN112876734A (en) * | 2021-01-13 | 2021-06-01 | 西北工业大学 | Method for recycling epoxy resin-based carbon fiber composite material under mild condition |
CN116396092A (en) * | 2023-04-07 | 2023-07-07 | 湖南远辉复合材料有限公司 | Preparation method of C/C composite material |
CN116396092B (en) * | 2023-04-07 | 2023-10-31 | 湖南远辉复合材料有限公司 | Preparation method of C/C composite material |
Also Published As
Publication number | Publication date |
---|---|
JPH0745574B2 (en) | 1995-05-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU747949B2 (en) | Process for preparing polyarylethers | |
US4654410A (en) | Aromatic polysulfone ether/polythioether sulfone copolymer and process for its preparation | |
EP0053344B1 (en) | Stabilized polyphenylene sulfide and method for producing same | |
US4812552A (en) | Process for preparing poly(arylene sulfide ketone) with water addition | |
KR20200090270A (en) | Method for producing polyphenylene sulfide resin and polyphenylene sulfide resin prepared accordingly | |
JP2004352923A (en) | Method for producing polyarylene sulfide resin | |
JPS63125531A (en) | Carbon fiber-reinforced resin composition | |
US4795799A (en) | Production of aromatic sulfide/ketone polymers with alkali metal carbonate | |
WO2019151288A1 (en) | Polyarylene sulfide copolymer and method for producing same | |
US4868275A (en) | Preparation of poly (arylene sulfide) from dihalo aromatic hydroxyl compound | |
JP2707118B2 (en) | Method for producing high molecular weight polyphenylene sulfide resin | |
JP2625856B2 (en) | Polyarylene thioether copolymer and method for producing the same | |
JPH0629319B2 (en) | Block copolymer | |
JP7214997B2 (en) | Method for producing carboxyalkylamino group-containing compound and method for producing cyclic polyarylene sulfide | |
JPS62119268A (en) | Carbon-fiber reinforced resin composition | |
JP7214998B2 (en) | Method for producing carboxyalkylamino group-containing compound and method for producing cyclic polyarylene sulfide | |
KR960006414B1 (en) | Aromatic sulfide amide polymer and the preparation process thereof | |
JPH04211926A (en) | Manufacture of heat-resistant resin molded product | |
JP2570721B2 (en) | Method for producing thermoplastic resin composition | |
JPH04202363A (en) | Polyarylene sulfide resin composition | |
JPS61247755A (en) | Resin composition | |
JP7214996B2 (en) | Method for producing carboxyalkylamino group-containing compound and method for producing cyclic polyarylene sulfide | |
JPS63130662A (en) | Thermoplastic resin composition | |
JPH04198267A (en) | Polyarylene sufide resin composition | |
EP0285874A1 (en) | Melt stabilization of polymers |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |