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JP4160771B2 - Fiber reinforced plastic molded body molding apparatus and molding method thereof - Google Patents
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JP4160771B2 - Fiber reinforced plastic molded body molding apparatus and molding method thereof - Google Patents

Fiber reinforced plastic molded body molding apparatus and molding method thereof Download PDF

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Publication number
JP4160771B2
JP4160771B2 JP2002116260A JP2002116260A JP4160771B2 JP 4160771 B2 JP4160771 B2 JP 4160771B2 JP 2002116260 A JP2002116260 A JP 2002116260A JP 2002116260 A JP2002116260 A JP 2002116260A JP 4160771 B2 JP4160771 B2 JP 4160771B2
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Prior art keywords
fiber material
sheet
molding
resin
bag film
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JP2003305733A5 (en
JP2003305733A (en
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秀博 竹本
巧 石森
喜春 沼田
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Mitsubishi Chemical Corp
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Mitsubishi Chemical Corp
Mitsubishi Rayon Co Ltd
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  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
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Description

【0001】
【発明の属する技術分野】
本発明は、繊維強化プラスチック(FRP)の成形装置とその成形方法に関し、具体的には成形型内に配されたシート状の強化繊維材料をバッグフィルムにて気密に被包し、バッグフィルム内を減圧しながら強化繊維材料にマトリックス樹脂を注入して成形する繊維強化プラスチックの真空注入成形装置とその成形方法に関する。
【0002】
【従来の技術】
FRP成形体は、スプレーアップ法やRTM法、プレス成形など、種々の方法により成形がなされているが、大型の成形体の場合はハンドレイアップ法にて成形されることが多かった。このハンドレイアップ法は、比較的古くから行われてきた成形方法であるが、強化繊維材料に対するマトッリクス樹脂の含浸の状態を人手で管理しているがため、その人員を確保することが難しく、作業中に逸散する臭気によって近隣に迷惑をかけたりするなどの問題があった。
【0003】
そこで、密閉された成形型に強化繊維材料を配するとともに真空圧下でマトリックス樹脂を注入する方法が考えられたが、樹脂がうまく含浸できないなどの問題が生じていた。これを改良するため、例えば特開2000−43172号公報では、発泡体からなるコア材の表裏両面に樹脂製の網状体を配するとともに、さらに各網状体の表面に強化繊維材料を配して、これらの全体をバッグフィルムで被包したのち、バッグフィルムで被包された内部を真空状態として、コア材の表面に形成された複数の溝を介してマトリックス樹脂を注入し、前記網状体の網目を通して強化繊維材料の表面方向に拡散させて、樹脂を強化繊維材料に含浸一体化させる方法を提案している。
【0004】
【発明が解決しようとする課題】
しかるに前記公報に開示されたFRPの成形方法では、マトリックス樹脂が強化繊維材料の全体に均等に含浸させるためには、コア材の表面に形成する溝のピッチを細かくしたりするなどの必要があり、その溝加工が煩雑であったり、真空で引かれて網状体を通ったマトリックス樹脂が強化繊維材料に含浸する途中で満たされると、強化繊維材料の表面側では真空による吸引力が全体に均等に働かず、強化繊維材料の表面側では樹脂含浸量が均等に含浸しなかったり、或いは真空による吸引力が樹脂の注入圧力を上回ると強化繊維材料の形状が保持できにくくなるという問題が生じる。
【0005】
本発明は、かかる課題を解決すべく開発されたものであり、その具体的な目的は真空吸引によるFRPの成形装置及び成形方法であっても、樹脂の含浸が強化繊維材料の全体にわたって均等になされるとともに、安定した形状が得られるFRPの成形装置とその成形方法を提供することにある。
【0006】
【課題を解決するための手段及び作用効果】
上記課題を解決すべくFRPの真空注入成形法について種々検討した結果、樹脂の含浸が良好で、且つ、生産性も良好な方法を発明するに至った。
【0007】
すなわち、本発明に係る成形装置の基本構成は、シート状の強化繊維材料が成形型の成形空間内に配され、同繊維材料を被包するバッグフィルムと、バッグフィルム内を減圧する減圧源と、前記繊維材料にマトリックス樹脂を注入する注入口とを有する繊維強化プラスチックの真空注入成形装置であって、前記成形空間の一面側が開放され、前記繊維材料の開放側表面と周縁が型に密封固定された前記バッグフィルムとの間に多数の小孔を有する多孔フィルムが配され、同多孔フィルムと前記バッグフィルムとの間に脱気回路を有する脱気用シートが配され、前記バッグフィルムと前記脱気用シートとの間の密閉空間に前記減圧源が接続され、前記繊維材料の前記多孔フィルムとは反対側の底部に向けて前記樹脂注入口が配されてなることを特徴とする繊維強化プラスチック成形体の成形装置にある。かかる構成により、樹脂含浸が良好で、且つ高い生産性をもたらす。
【0008】
ここで用いられる成形型の材質は、金属製、繊維強化樹脂製、樹脂製、木製のいずれであってもよく、用いるマトリックス樹脂の硬化温度によって適切に選択すればよい。また、その型形状は成形体の形状により決まる。しかして、成形にあたってはシート状の強化繊維材料の片面全面をバッグフィルムで被包する。前記シート状強化繊維材料は単層である必要はなく多層に積層されたものであってもよく、更には積層される繊維材料が同一の材質でなくてもよい。また同シート状繊維材料の内部に所望の形状をもつコア材を介装することも可能である。コア材には様々な合成樹脂が採用でき、更なる軽量化が必要な場合には発泡体とすることが好ましい。また、コア材の他にも、例えば金属製の機械部品を強化繊維材料に添装又は介装することもある。
【0009】
このとき用いられるバッグフィルムは、この種の真空注入成形法に一般に用いられる気密な合成樹脂製のフィルムであれば制限されない。このバッグフィルムは成形空間内の減圧が保持されるように、その周縁をシールテープや粘着材料などにより成形型に気密に固定する。また上記多孔フィルムは、その内側表面にフッ素樹脂などを配して離型性を備えさせることが好ましいが、その材質はマトリックス樹脂と非接着性材料であれば特に限定されない。
【0010】
この多孔フィルムに形成される孔の開口面積は2〜1000mm2 /m2 であり、これ以下では、真空吸引の効果が得られず、これ以上であると樹脂の吸い上げが著しくなり、真空吸引の効果が低くなる。また孔の開口数は、前述の範囲で1m2 当たり100個以下であることが望ましく、100個以上の場合には、樹脂の吸い上げに伴い脱気用シートの閉塞が発生し、良好な含浸特性が得られない。
【0011】
前記脱気回路用の脱気用シートには、成形空間内を減圧するため、真空が引けるように真空ポンプ等の減圧源に接続する吸引口が設けられている。この脱気用シートの材質は、特に規定しないが、ナイロン繊維やガラス繊維等が挙げられ、織組織について規定しないが織布や不織布が挙げられる。このシートの目付についても特に規定しないが、使用減圧下での吸引回路が確保できるようなものを選択する。そのためには、上記多孔フィルムと同様に、構成繊維材料としてはマトリックス樹脂に対する非接着性の材料であることが望ましい。
【0012】
この状態で、真空吸引による減圧環境下で樹脂注入口よりマトリックス樹脂を注入し、成形体を得る。この樹脂注入時の粘度は20Poise 以下であることが必要であり、これを超えるような粘度では、シート状強化繊維材料に対して樹脂の未含浸部分が発生する可能性があるため不適当である。用いられる樹脂の種類としては特に規定しないが、エポキシ樹脂,ビニルエステル樹脂,不飽和ポリエステル樹脂,フェノール樹脂等の熱硬化性樹脂が挙げられる。
【0013】
また、シート状強化繊維材料の材質としては、炭素繊維製織物、同繊維製不織布、炭素繊維トウや、ガラス繊維製織物、その不織布、ロービングを、単独で又は組合せて、あるいは炭素線,糸ガラス繊維とを混合して使用することが好ましい。特に軽量化と強度を得るには炭素繊維の使用が好ましい。複数の炭素繊維トウを拡幅してシートを形成するときは、積層する繊維の配向を変えて積層すれば、全ての方向に所望の機械特性が得られるため好ましい。通常、炭素繊維トウ1本のフィラメント数は10,000〜300,000本の範囲、より好ましくは50,000〜150,000本の範囲にある。
【0014】
本発明に係るFRP成形体は、既述したとおり、シート状の強化繊維材料単独、或いは強化繊維材料の間にコア材を介装させた構造体を含んでいる。これらの強化繊維材料及びコア材の全体を、多孔フィルム、脱気用シート、バッグフイルムの順で内側から順次被包し、脱気用シートを介してバッグフイルムで覆われた内部を減圧状態として、マトリックス樹脂を強化繊維材料の底部に注入し、吸引により前記強化繊維材料を介して前記強化繊維材料の面方向に拡散させ、該樹脂を強化繊維材料に満遍なく含浸させることにより全体を一体に成形する。このとき、多孔フィルムと脱気用シートは、脱気用シートを介して吸引される成形空間内の気体の流れが脱気用シートと多孔フィルムによって分散され、強化繊維材料の全体にわたり均等な吸引力が働き、注入されたマトリックス樹脂を強化繊維材料の内部に均等に含浸させるようになる。
【0015】
その成形方法にあって、開閉可能な上下型を用いずに、一面側が開放する金型を単独で用いるときは、その開放側に上記多孔フィルム、脱気用シート、バッグフイルムの順に積層し、バッグフィルムの周縁をシール材を介して型に固着し、型と多孔フィルムとの間に形成される空間を密閉された成形空間とし、その密閉空間に強化繊維材料を配置する。内部をコア材を介装するときは、そのコア材の外形が型材の型面をなし、シート状の強化繊維材料を介して被包される上記多孔フィルム、脱気用シート、バッグフイルムが自由に形態変化できるため、成形される構造体もコア材の外形に追従することになる。
【0016】
脱気用シートを介して成形空間内の気体を吸引すると、強化繊維材料の内部の気体をも含めて、多孔フィルムの孔を通って外部に引かれ、同時に繊維材料に向けて注入されるマトリックス樹脂は、繊維材料内を満遍なく拡散して強化繊維材料の全体に含浸する。このとき、脱気回路をもつ脱気用シートは、既述したごとく、多孔フィルムを介してシート全体にわたって均一に吸気しており、その吸気により成形空間内の圧力が所定の値まで減圧される。この減圧状態が維持されている間に、注入された所要量のマトリックス樹脂は繊維材料の全体にわたり均一に拡散して含浸する。すなわち、強化繊維材料へのマトリックス樹脂の含浸が極めて円滑にかつ均一に行われ、高品質のFRP構造体が安定して効率的に、しかも安価に製造される。
【0018】
【発明の実施の形態】
以下に、本発明の望ましい実施の形態を、図面に基づいて具体的に説明する。図1は本発明の第1実施形態である長尺の平板状FRP成形体を真空注入成形時の状態を模式的に示している。
【0019】
本実施形態による平板状FRP成形体の真空注入成形装置は、水平に配された平板状の成形型1と、所要の成形空間を設けて前記成形型1の上面に配される多孔フィルム2と、同多孔フィルム2の上面に配される脱気シート3と、同脱気シート3の更に上面に配されるバッグフィルム4とを備えている。成形時には、最内層の前記多孔フィルム2と前記平板状型1との間に形成される成形空間内には平板状の強化繊維材料5が介装され、同強化繊維材料5を介装したのち、前記脱気シート3及びバッグフィルム4の周縁を、シール材6を介して前記成形型1の上面に密封固定する。
【0020】
一方、上記平板状の成形型1にはマトリックス樹脂の注入口1aが貫通して形成されており、同注入孔1aの上端は樋状の溝1bとなって成形型1の長手方向に延びている。この樹脂注入口1aは外部の図示せぬ樹脂貯留槽と配管を介して接続されている。また、前記脱気シート3の周縁部の一部に成形空間内の気体を吸引する吸気口7が形成されており、この吸気口7はバッグフィルムを介して外部に配設された真空ポンプ8の吸気ポートに配管9を介して接続されている。ここで、脱気シート3にはナイロン繊維やガラス繊維から構成される織布や不織布が使われ、上記多孔フィルム2と併用することにより吸引空気に一方向の流れを生じさせることなく、強化繊維材料の全面に均一な吸気流れを発生させる。
【0021】
多孔フィルム2に形成される孔の開口面積は、真空吸引の効果が得られる2〜1000mm2 /m2 とすることが好ましく、また孔の開口数も、前述の範囲で1m2 当たり100個以下であることが望ましい。100個以上の場合には、樹脂の吸い上げに伴い脱気用シートの閉塞が発生し、良好な含浸特性が得られない。FRPのマトリックス樹脂として、エポキシ、不飽和ポリエステル、フェノール、ビニルエステルなどの熱硬化性樹脂が使われる。勿論、ポリエステルやナイロン、ABS樹脂等の熱可塑性樹脂を単独で、或いはそれらと熱硬化性樹脂との混合樹脂も使用が可能である。
【0022】
図2は、本発明の第2実施形態を模式的に示している。本実施形態による成形型10は、内部に成形空間を有するとともに、その上面が外部に開放された箱型形態を備えている。本実施形態にあっては、強化繊維材料15の間にコア材16を介装させている。所望の形状をもつコア材16の上面に第1の強化繊維材料15aを載置すると共に、コア材16の側面と下面とを被覆するように第2の繊維強化材料15aを配し、これを前記成形型10の成形空間に収容する。コア材としては、軽量化には硬質の発泡体やコルク等を使用することが好ましく、またアルミ材からなるハニカムを使うこともできる。本実施形態によるコア材16には、その中央部に上下に貫通する樹脂流通孔16aが形成されている。
【0023】
この状態で、上記第1実施形態例と同様に、内側から多孔フィルム12、脱気用シート13及びバッグフィルム14を順次積層し、多孔フィルム12及び脱気用シート13の周縁をシール材11を介して密封固定する。多孔フィルム12には、同じく上記第1実施形態と同様に、多数の孔が開けられており、脱気用シート13の周縁の一部に吸気口17が形成され、バッグフィルム14を介して外部に設置された真空ポンプ18の吸入ポートに配管19を介して接続されている。また、本実施形態では前記多孔フィルム12、脱気用シート13及びバッグフィルム14を順次貫いて、前記箱型の成形型10の底面に向けたマトリックス樹脂の管状注入口10aが配され、同注入口10aが図示せぬ配管を介して同じく図示せぬマトリックス樹脂槽に接続されている。
【0024】
いま、吸気口17から吸気することにより、成形空間内は減圧化される。この吸気を持続しながら、前記管状注入口10aを介してマトリックス樹脂が成形型10の底部に配された第2強化繊維材料15bへと注入される。脱気用シート13の周縁の一部に形成された吸気口17から、成形空間内の気体を吸気すると、多孔フィルム12の存在により、吸気される気体は一方向に流れずに、多孔フィルム12に形成された多数の孔を通して均等に吸気される。そのため、その吸引力も繊維材料の全体にわたって均等になされ、前述のように、下部強化繊維材料15bに注入されたマトリックス樹脂は、同第2強化繊維材料15bの全体にわたって吸引拡散し、第1強化繊維材料15aに達する。このときも、吸引力は第1強化繊維材料15aの全体に均等に働くため、マトリックス樹脂は上部強化繊維材料15aにも均等に吸引されて行き渡り含浸する。
【0025】
本実施形態ではコア材16の全面を強化繊維材料15で被包しているが、コア材16の片面を外部に露呈し、或いはコア材16の上下の面にだけ繊維材料15を配することもできる。
【0026】
次に、本発明の実施例に基づいて、より具体的に説明する。
[実施例1]
長さ1. 8m,幅0. 9mでその一辺に樹脂注入用の長溝が形成された、図1に示す平板状成形型に対して、基材A(ガラスチョップドストランドマット:225g/m2 )/基材B(三菱レイヨン製炭素繊維織物:TRK910)/基材Aの順で生機を配置した。次に200mm間隔で1mmφ程度の孔を27個開口したフィルム(デュポン社製テドラフィルム)をその上より覆い、各周縁部をシール材にて粘着固定した。この孔を開けた多孔フィルムについて測定したところ、1m2 当たりの開口面積が13. 09mm2 、開口数が16. 7個/m2 であった。
【0027】
次に、脱気回路用の脱気シート(ガラス製織物:目付250g/m2 )をその上より被せた。更にその上からバッグフィルム(Airtech社製ナイロンフィルム 厚み0.002inch)を被せてシール材に粘着固定した。その後、樹脂の注入口とは反対側のバッグフィルムに真空引き用の吸気口を配管を介して真空ポンプに接続した。次に、真空ポンプを稼動させ、所定の減圧が保持されるようにバッグフィルムとシール材の気密性を確認し、約30分間、750mmHgの減圧状態を保持した。このとき、マトリックス樹脂の注入口は閉じられたままであり、空気が入り込まないようにした。
【0028】
次に、22℃での粘度が10poiseである常温硬化タイプのビニルエステル樹脂を用いて、樹脂注入口より注入を開始した。注入時の真空圧力は300mmHgとし、樹脂注入方法は自然落下方式を採用し、無真空状態での注入口での注入圧力範囲が0. 05〜0. 01MPaとなるようにした。所定の樹脂注入量でマトリックス樹脂を注入完了後、注入口を閉鎖し樹脂注入を停止した。その後、真空圧力を500mmHgまで減圧保持し、樹脂を硬化させた。
得られた積層板は、樹脂の未含浸部分がほとんど無い表面状態の良好な成形板であった。
【0029】
[実施例2]
長さ3. 0m,幅2. 4mの図2に示す成形型に対して、基材A(ガラスチョップドストランドマット:225g/m2 )/基材B(三菱レイヨン製炭素繊維織物:TRK910)/基材Aの順で構成された第2強化繊維材料からなる第2スキン層を配置した。更にその上より、コア材を配置し、第2スキン層と同様の手順で基材A/基材B/基材Aを順次積層した第1強化繊維材料からなる第1スキン層を配置した。次に、約500mm間隔で3mmφ程度の孔を42個開口したフィルム(デュポン社製テドラフィルム)をその上から覆い、同多孔フィルムの周縁部をシール材にて粘着固定した。この孔が開けられたフィルムについて測定したところ、1m2 当たり開口面積で41. 23mm2 および開口数が約5. 8個/m2 であった。
【0030】
次に、脱気用シート(ガラス製織物:目付250g/m2 )をその上から被せた。更に、その上よりバッグフィルム(Airtech社製ナイロンフィルム 厚み0.002inch)を被せてシール材に粘着固定した。その後、長さ方向の一辺に樹脂の注入口を約500mm間隔で7個設け、それとは反対側のバッグフィルムの端部に真空引き用の吸気口を開け、そこに配管を介して真空ポンプに接続した。次に、真空ポンプを稼動させ、減圧が保持されるようにバッグフィルムとシール材の気密性を確認し、約60分間、750mmHgの常圧状態を保持した。このとき、各樹脂注入口は閉じられたままであって、空気が入り込まないようにした。
【0031】
次に、25℃での粘度が5poiseである常温硬化タイプのビニルエステル樹脂を用いて、樹脂注入口より樹脂の注入を開始した。注入時の真空圧力は400mmHgとし、樹脂注入方法は自然落下方式を採用し、減圧状態にある注入口での注入圧力範囲を0. 05〜0. 01MPaとなるようにした。所定の樹脂注入量が注入された後、順次、注入口を閉鎖して樹脂の注入を停止した。その後、真空圧力を650mmHgに減圧保持し、マトリックス樹脂を硬化させた。
得られたサンドイッチ積層板の未含浸の状態を超音波により測定したところ、ほとんどに樹脂が含浸している表面状態の良好なサンドイッチ成形体が得られていることが分かった。
【0032】
このように、本発明によれば、従来問題であった樹脂の未含浸部分がほとんど無くなり、臭気も少なく生産性の優れた成形が可能となった。
【図面の簡単な説明】
【図1】本発明の第1実施形態に係るFRP成形時の成形状態を模式的に示す断面図である。
【図2】本発明の第2実施形態に係るFRP成形時の成形状態を模式的に示す断面図である。
【符号の説明】
1,10 成形型
1a 樹脂注入口
1b 溝
10a 管状注入口
2,12 多孔フィルム
3,13 脱気用シート
4,14 バッグフィルム
5,15 強化繊維材料
15a,15b 上下部強化繊維材料
6 シール材
7,17 吸気口
8,18 真空ポンプ
9,19 配管
11 シール材
16 コア材
16a 樹脂流通孔
[0001]
BACKGROUND OF THE INVENTION
TECHNICAL FIELD The present invention relates to a fiber reinforced plastic (FRP) molding apparatus and a molding method thereof. Specifically, a sheet-like reinforcing fiber material arranged in a mold is hermetically encapsulated with a bag film, The present invention relates to a vacuum injection molding apparatus and a molding method for fiber reinforced plastics, in which a matrix resin is injected into a reinforced fiber material while reducing pressure.
[0002]
[Prior art]
The FRP molded body is molded by various methods such as spray-up method, RTM method, press molding, etc., but in the case of a large molded body, it is often molded by the hand lay-up method. This hand lay-up method is a molding method that has been performed for a relatively long time, but because the state of impregnation of the matrix resin to the reinforcing fiber material is managed manually, it is difficult to secure the personnel, There were problems such as inconvenience to the neighborhood due to odors that dissipated during work.
[0003]
Therefore, a method of arranging a reinforcing fiber material in a sealed mold and injecting a matrix resin under a vacuum pressure has been considered, but there has been a problem that the resin cannot be impregnated well. In order to improve this, for example, in Japanese Patent Laid-Open No. 2000-43172, a resin mesh is arranged on both the front and back surfaces of a core material made of foam, and a reinforcing fiber material is arranged on the surface of each mesh. Then, after encapsulating the whole with a bag film, the interior encapsulated with the bag film is in a vacuum state, and a matrix resin is injected through a plurality of grooves formed on the surface of the core material. A method of impregnating and integrating a resin into a reinforcing fiber material by diffusing in the surface direction of the reinforcing fiber material through a mesh is proposed.
[0004]
[Problems to be solved by the invention]
However, in the FRP molding method disclosed in the above publication, in order for the matrix resin to uniformly impregnate the entire reinforcing fiber material, it is necessary to reduce the pitch of grooves formed on the surface of the core material. If the groove processing is complicated, or the matrix resin that has been drawn in a vacuum and passed through the network is filled in the middle of impregnating the reinforcing fiber material, the suction force by the vacuum is evenly distributed on the surface side of the reinforcing fiber material. However, if the resin impregnation amount is not uniformly impregnated on the surface side of the reinforcing fiber material, or if the suction force by the vacuum exceeds the injection pressure of the resin, there arises a problem that it becomes difficult to maintain the shape of the reinforcing fiber material.
[0005]
The present invention has been developed to solve such a problem. Even if the specific object is a FRP molding apparatus and molding method by vacuum suction, the impregnation of the resin is evenly distributed over the entire reinforcing fiber material. Another object of the present invention is to provide an FRP molding apparatus and a molding method thereof that can achieve a stable shape.
[0006]
[Means for solving the problems and effects]
As a result of various investigations on the vacuum injection molding method of FRP in order to solve the above problems, the inventors have invented a method with good resin impregnation and good productivity.
[0007]
That is, the basic configuration of the molding apparatus according to the present invention includes a bag film in which a sheet-like reinforcing fiber material is disposed in a molding space of a mold, and a vacuum source that depressurizes the bag film. A vacuum injection molding apparatus for fiber reinforced plastic having an injection port for injecting a matrix resin into the fiber material, wherein one side of the molding space is opened, and the open side surface and periphery of the fiber material are sealed in a mold A porous film having a large number of small holes is disposed between the fixed bag film, and a degassing sheet having a degassing circuit is disposed between the porous film and the bag film. wherein said vacuum source is connected to the closed space between the deaerating sheet, to become arranged that the resin injection port toward the bottom of the opposite side of the porous film of the fiber material In the molding apparatus of a fiber reinforced plastic molding according to symptoms. With this configuration, resin impregnation is good and high productivity is achieved.
[0008]
The material of the mold used here may be any of metal, fiber reinforced resin, resin, and wood, and may be appropriately selected depending on the curing temperature of the matrix resin to be used. The mold shape is determined by the shape of the molded body. For molding, the entire surface of one side of the sheet-like reinforcing fiber material is encapsulated with a bag film. The sheet-like reinforcing fiber material does not need to be a single layer and may be laminated in multiple layers, and the fiber materials to be laminated may not be the same material. It is also possible to interpose a core material having a desired shape inside the sheet-like fiber material. Various synthetic resins can be used as the core material, and when further weight reduction is required, a foam is preferable. In addition to the core material, for example, metal mechanical parts may be attached to or interposed in the reinforcing fiber material.
[0009]
The bag film used at this time is not limited as long as it is an airtight synthetic resin film generally used in this type of vacuum injection molding method. The bag film is hermetically fixed to the mold with a sealing tape or an adhesive material so that the reduced pressure in the molding space is maintained. The porous film is preferably provided with a release property by arranging a fluororesin or the like on the inner surface thereof, but the material is not particularly limited as long as the material is a matrix resin and a non-adhesive material.
[0010]
The opening area of the holes formed in the porous film is 2 to 1000 mm 2 / m 2 , and below this, the effect of vacuum suction cannot be obtained. Less effective. In addition, the number of apertures in the hole is desirably 100 or less per 1 m 2 within the above-mentioned range. When the number is 100 or more, the degassing sheet is blocked as the resin is sucked up, and good impregnation characteristics are obtained. Cannot be obtained.
[0011]
The degassing sheet for the degassing circuit is provided with a suction port connected to a pressure reducing source such as a vacuum pump so as to draw a vacuum in order to depressurize the molding space. The material of the deaeration sheet is not particularly defined, but examples thereof include nylon fiber and glass fiber, and the woven structure is not defined, but woven fabric and nonwoven fabric are exemplified. The basis weight of the sheet is not particularly defined, but a sheet that can secure a suction circuit under a use reduced pressure is selected. For this purpose, as in the case of the porous film, it is desirable that the constituent fiber material is a non-adhesive material for the matrix resin.
[0012]
In this state, a matrix resin is injected from the resin injection port under a reduced pressure environment by vacuum suction to obtain a molded body. The viscosity at the time of resin injection needs to be 20 Poise or less, and a viscosity exceeding this value is unsuitable because an unimpregnated portion of the resin may occur in the sheet-like reinforcing fiber material. . Although it does not prescribe | regulate especially as a kind of resin used, Thermosetting resins, such as an epoxy resin, vinyl ester resin, unsaturated polyester resin, a phenol resin, are mentioned.
[0013]
In addition, as the material of the sheet-like reinforcing fiber material, carbon fiber woven fabric, non-woven fabric made of the same fiber, carbon fiber tow, glass fiber woven fabric, non-woven fabric, roving, alone or in combination, carbon wire, yarn glass It is preferable to mix and use the fiber. In particular, the use of carbon fiber is preferred for obtaining light weight and strength. When a sheet is formed by widening a plurality of carbon fiber tows, it is preferable to stack by changing the orientation of the fibers to be laminated because desired mechanical properties can be obtained in all directions. Usually, the number of filaments of one carbon fiber tow is in the range of 10,000 to 300,000, more preferably in the range of 50,000 to 150,000.
[0014]
As described above, the FRP molded body according to the present invention includes a sheet-like reinforcing fiber material alone or a structure in which a core material is interposed between reinforcing fiber materials. The whole of these reinforcing fiber materials and core materials are encapsulated sequentially from the inside in the order of a porous film, a deaeration sheet, and a bag film, and the inside covered with the bag film through the deaeration sheet is in a reduced pressure state. The matrix resin is injected into the bottom of the reinforcing fiber material, diffused in the surface direction of the reinforcing fiber material through the reinforcing fiber material by suction, and the resin is evenly impregnated into the reinforcing fiber material so that the whole is integrally molded To do. At this time, in the porous film and the degassing sheet, the gas flow in the molding space sucked through the degassing sheet is dispersed by the degassing sheet and the porous film, and uniform suction is performed throughout the reinforcing fiber material. The force works, so that the injected matrix resin is uniformly impregnated inside the reinforcing fiber material.
[0015]
In the molding method, without using the upper and lower molds that can be opened and closed, when using a mold that opens on one side alone, the porous film, degassing sheet, and bag film are laminated in that order on the open side, The periphery of the bag film is fixed to the mold through a sealing material, and the space formed between the mold and the porous film is defined as a sealed molding space, and the reinforcing fiber material is disposed in the sealed space. When interposing a core material inside, the outer shape of the core material forms the surface of the mold material, and the porous film, deaeration sheet, and bag film that are encapsulated via the sheet-like reinforcing fiber material are free. Therefore, the structure to be molded follows the outer shape of the core material.
[0016]
When the gas in the molding space is sucked through the degassing sheet, the matrix is drawn to the outside through the pores of the porous film, including the gas inside the reinforcing fiber material, and simultaneously injected toward the fiber material. The resin diffuses evenly in the fiber material and impregnates the entire reinforcing fiber material. At this time, as described above, the deaeration sheet having the deaeration circuit sucks air uniformly throughout the sheet through the porous film, and the pressure in the molding space is reduced to a predetermined value by the intake air. . While this reduced pressure is maintained, the required amount of injected matrix resin diffuses and impregnates uniformly throughout the fiber material. That is, the reinforcing fiber material is impregnated with the matrix resin very smoothly and uniformly, and a high-quality FRP structure is stably and efficiently manufactured at low cost.
[0018]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be specifically described with reference to the drawings. FIG. 1 schematically shows a state of a long flat plate-shaped FRP molded body according to the first embodiment of the present invention during vacuum injection molding.
[0019]
The flat injection molding apparatus for a flat FRP molded body according to the present embodiment includes a flat plate-shaped mold 1 arranged horizontally, a porous film 2 provided on the upper surface of the mold 1 with a required molding space, and The degassing sheet 3 disposed on the upper surface of the porous film 2 and the bag film 4 disposed on the upper surface of the degassing sheet 3 are provided. At the time of molding, a flat reinforcing fiber material 5 is interposed in the forming space formed between the innermost porous film 2 and the flat plate mold 1, and after the reinforcing fiber material 5 is interposed. The peripheral edges of the deaeration sheet 3 and the bag film 4 are hermetically fixed to the upper surface of the mold 1 with a sealing material 6 interposed therebetween.
[0020]
On the other hand, a matrix resin injection port 1 a is formed through the flat plate-shaped mold 1, and the upper end of the injection hole 1 a becomes a bowl-shaped groove 1 b and extends in the longitudinal direction of the mold 1. Yes. The resin inlet 1a is connected to an external resin storage tank (not shown) through a pipe. An air inlet 7 for sucking the gas in the molding space is formed in a part of the peripheral edge of the deaeration sheet 3, and the air inlet 7 is provided outside via a bag film. The intake port is connected via a pipe 9. Here, a woven fabric or a non-woven fabric made of nylon fiber or glass fiber is used for the deaeration sheet 3, and it is used in combination with the porous film 2 to reinforce the reinforced fiber without causing unidirectional flow in the suction air. A uniform intake flow is generated over the entire surface of the material.
[0021]
The opening area of the holes formed in the porous film 2 is preferably 2 to 1000 mm 2 / m 2 where the effect of vacuum suction is obtained, and the number of holes is 100 or less per 1 m 2 within the above-mentioned range. It is desirable that When the number is 100 or more, the degassing sheet is blocked as the resin is sucked up, and good impregnation characteristics cannot be obtained. Thermosetting resins such as epoxy, unsaturated polyester, phenol, and vinyl ester are used as matrix resin for FRP. Of course, thermoplastic resins such as polyester, nylon, and ABS resin can be used alone, or a mixed resin of these and a thermosetting resin can be used.
[0022]
FIG. 2 schematically shows a second embodiment of the present invention. The mold 10 according to the present embodiment has a box shape with a molding space inside and an upper surface opened to the outside. In the present embodiment, the core material 16 is interposed between the reinforcing fiber materials 15. The first reinforcing fiber material 15a is placed on the upper surface of the core material 16 having a desired shape, and the second fiber reinforcing material 15a is disposed so as to cover the side surface and the lower surface of the core material 16, and this The mold 10 is accommodated in a molding space. As the core material, it is preferable to use a hard foam or cork for weight reduction, and a honeycomb made of an aluminum material can also be used. The core material 16 according to the present embodiment is formed with a resin flow hole 16a penetrating vertically in the center thereof.
[0023]
In this state, similarly to the first embodiment, the porous film 12, the degassing sheet 13 and the bag film 14 are sequentially laminated from the inside, and the peripheral edges of the porous film 12 and the degassing sheet 13 are sealed with the sealing material 11. Through the seal. Similarly to the first embodiment, the porous film 12 is provided with a large number of holes, and an air inlet 17 is formed in a part of the peripheral edge of the deaeration sheet 13, and is externally passed through the bag film 14. Is connected to a suction port of a vacuum pump 18 installed in a pipe 19 via a pipe 19. Further, in the present embodiment, a tubular resin inlet 10a of a matrix resin is arranged through the porous film 12, the degassing sheet 13 and the bag film 14 in this order toward the bottom of the box-shaped mold 10, and the same note. The inlet 10a is connected to a matrix resin tank (not shown) through a pipe (not shown).
[0024]
Now, by taking in air from the air inlet 17, the inside of the molding space is decompressed. While continuing this suction, the matrix resin is injected into the second reinforcing fiber material 15b disposed at the bottom of the mold 10 through the tubular injection port 10a. When the gas in the molding space is sucked from the suction port 17 formed at a part of the periphery of the degassing sheet 13, the sucked gas does not flow in one direction due to the presence of the porous film 12. The air is evenly sucked through a large number of holes formed in the. Therefore, the suction force is also made uniform throughout the fiber material, and as described above, the matrix resin injected into the lower reinforcing fiber material 15b is sucked and diffused throughout the second reinforcing fiber material 15b, and the first reinforcing fibers Reach material 15a. Also at this time, the suction force acts evenly on the entire first reinforcing fiber material 15a, so that the matrix resin is evenly sucked into the upper reinforcing fiber material 15a and is spread and impregnated.
[0025]
In this embodiment, the entire surface of the core material 16 is encapsulated with the reinforcing fiber material 15, but one surface of the core material 16 is exposed to the outside, or the fiber material 15 is disposed only on the upper and lower surfaces of the core material 16. You can also.
[0026]
Next, based on the Example of this invention, it demonstrates more concretely.
[Example 1]
1. A substrate A (glass chopped strand mat: 225 g / m 2 ) with respect to the flat plate mold shown in FIG. 1 having a length of 1.8 m, a width of 0.9 m and a long groove for resin injection formed on one side thereof. The raw machine was arranged in the order of: / base material B (carbon fiber fabric manufactured by Mitsubishi Rayon: TRK910) / base material A. Next, a film (Tedola film made by DuPont) having 27 holes of about 1 mmφ at 200 mm intervals was covered from above, and each peripheral edge was adhesively fixed with a sealing material. When the porous film having the holes was measured, the opening area per 1 m 2 was 13.09 mm 2 and the numerical aperture was 16.7 pieces / m 2 .
[0027]
Next, a deaeration sheet for a deaeration circuit (glass fabric: basis weight 250 g / m 2 ) was placed thereon. Further, a bag film (Nylon film manufactured by Airtech Co., Ltd., thickness 0.002 inch) was placed on the sealing material to fix it to the sealing material. Thereafter, a suction port for evacuation was connected to a vacuum pump through a pipe in the bag film opposite to the resin inlet. Next, the vacuum pump was operated to check the airtightness of the bag film and the sealing material so that a predetermined reduced pressure was maintained, and the reduced pressure state of 750 mmHg was maintained for about 30 minutes. At this time, the matrix resin inlet was kept closed so that air could not enter.
[0028]
Next, injection | pouring was started from the resin injection port using the normal temperature hardening type vinyl ester resin whose viscosity in 22 degreeC is 10 poise. The vacuum pressure at the time of pouring was 300 mmHg, and the natural pouring method was adopted as the resin pouring method so that the pouring pressure range at the pouring port in a non-vacuum state was 0.05 to 0.01 MPa. After completing the matrix resin injection at a predetermined resin injection amount, the injection port was closed and the resin injection was stopped. Thereafter, the vacuum pressure was reduced to 500 mmHg to cure the resin.
The obtained laminated plate was a molded plate having a good surface state with almost no unimpregnated portion of resin.
[0029]
[Example 2]
For the mold shown in FIG. 2 having a length of 3.0 m and a width of 2.4 m, base material A (glass chopped strand mat: 225 g / m 2 ) / base material B (carbon fiber fabric manufactured by Mitsubishi Rayon: TRK910) / The 2nd skin layer which consists of the 2nd reinforcement fiber material comprised in order of the base material A was arrange | positioned. Further, a core material was disposed thereon, and a first skin layer made of a first reinforcing fiber material in which the base material A / the base material B / the base material A were sequentially laminated in the same procedure as the second skin layer was disposed. Next, a film (Tedola film made by DuPont) having 42 holes of about 3 mmφ opened at intervals of about 500 mm was covered from above, and the periphery of the porous film was adhesively fixed with a sealing material. As a result of measuring the film with the holes, the opening area per 1 m 2 was 41.23 mm 2 and the numerical aperture was about 5.8 / m 2 .
[0030]
Next, a sheet for deaeration (glass fabric: basis weight 250 g / m 2 ) was placed thereon. Furthermore, a bag film (Nylon film made by Airtech Co., Ltd., thickness 0.002 inch) was placed on the sealing material and adhered to the sealing material. After that, seven resin injection ports are provided at intervals of about 500 mm on one side in the length direction, and an air suction port is opened at the end of the bag film on the opposite side, and a vacuum pump is connected there through a pipe. Connected. Next, the vacuum pump was operated, the airtightness of the bag film and the sealing material was confirmed so that the reduced pressure was maintained, and the normal pressure state of 750 mmHg was maintained for about 60 minutes. At this time, each resin inlet was kept closed so that air could not enter.
[0031]
Next, injection of the resin was started from the resin injection port using a normal temperature curing type vinyl ester resin having a viscosity at 25 ° C. of 5 poise. The vacuum pressure at the time of pouring was 400 mmHg, the natural pouring method was adopted as the resin pouring method, and the pouring pressure range at the pouring port in a reduced pressure state was set to 0.05 to 0.01 MPa. After a predetermined resin injection amount was injected, the injection port was sequentially closed to stop the resin injection. Thereafter, the vacuum pressure was kept at 650 mmHg to cure the matrix resin.
When an unimpregnated state of the obtained sandwich laminate was measured by ultrasonic waves, it was found that a sandwich molded body having a good surface state in which the resin was almost impregnated was obtained.
[0032]
As described above, according to the present invention, the unimpregnated portion of the resin, which has been a problem in the past, is almost eliminated, and molding with less odor and excellent productivity is possible.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view schematically showing a molding state during FRP molding according to a first embodiment of the present invention.
FIG. 2 is a cross-sectional view schematically showing a molding state during FRP molding according to a second embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1,10 Mold 1a Resin injection port 1b Groove 10a Tubular injection port 2,12 Porous film 3,13 Deaeration sheet 4,14 Bag film 5,15 Reinforcement fiber material 15a, 15b Upper and lower reinforcement fiber material 6 Sealing material 7 , 17 Intake port 8, 18 Vacuum pump 9, 19 Piping 11 Sealing material 16 Core material 16a Resin flow hole

Claims (8)

シート状の強化繊維材料が成形型の成形空間内に配され、同繊維材料を被包するバッグフィルムと、バッグフィルム内を減圧する減圧源と、前記繊維材料にマトリックス樹脂を注入する注入口とを有する繊維強化プラスチックの真空注入成形装置であって、
前記成形空間の一面側が開放され、
前記繊維材料の開放側表面と周縁が型に密封固定された前記バッグフィルムとの間に多数の小孔を有する多孔フィルムが配され、
同多孔フィルムと前記バッグフィルムとの間に脱気回路を有する脱気用シートが配され、
前記バッグフィルムと前記脱気用シートとの間の密閉空間に前記減圧源が接続され、
前記繊維材料の前記多孔フィルムとは反対側の底部に向けて前記樹脂注入口が配されてなる、
ことを特徴とする繊維強化プラスチック成形体の成形装置。
A bag film in which a sheet-like reinforcing fiber material is arranged in the molding space of the mold and encapsulates the fiber material, a reduced pressure source for depressurizing the bag film, and an inlet for injecting a matrix resin into the fiber material A vacuum injection molding apparatus for fiber-reinforced plastic having
One side of the molding space is opened,
A porous film having a large number of small holes is disposed between the open side surface of the fiber material and the bag film whose periphery is hermetically fixed to a mold ,
A degassing sheet having a degassing circuit is disposed between the porous film and the bag film,
The reduced pressure source is connected to a sealed space between the bag film and the degassing sheet,
The resin injection port is arranged toward the bottom of the fiber material opposite to the porous film,
An apparatus for molding a fiber-reinforced plastic molded product.
前記脱気用シートがガラス繊維織物である請求項1記載の成形装置。  The molding apparatus according to claim 1, wherein the degassing sheet is a glass fiber fabric. 前記多孔フィルムが1m2 あたりに2〜1000mm2 の開口面積を有してなることを特徴とする請求項1又は2に記載の成形装置。The porous film forming apparatus according to claim 1 or 2, characterized by having an opening area of 2~1000Mm 2 per 1 m 2. 前記多孔フィルムが1m2 あたりに100個以下で孔を有してなることを特徴とする請求項1〜3のいずれかに記載の成形装置。The forming device according to claim 1, wherein the porous film has 100 or less holes per 1 m 2 . シート状の強化繊維材料を成形型の成形空間内に配し、同繊維材料をバッグフィルムにて気密に被包し、前記繊維材料にマトリックス樹脂を注入するとともに、バッグフィルム内を減圧して、繊維強化プラスチックを成形する真空注入成形方法にあって、
前記成形空間の一面を開放すること、
前記成形型内に強化繊維材料を配すること、
同繊維材料の表面多数の小孔を有する多孔フィルムにて配すること、
多孔フィルムの表面側に脱気回路を有する脱気用シートを配すること、
バッグフィルムを成形空間内が密閉状態となるように前記脱気用シートの表面側に配すること、
外部の減圧源により前記脱気用シートを介して成形空間内を減圧下におくこと、及び
減圧下にある成形空間内の前記繊維材料の底部に、樹脂注入時の樹脂粘度が20Poise 以下であるマトリックス樹脂を注入すること、
を含んでなることを特徴とする繊維強化プラスチック成形体の成形方法。
A sheet-like reinforcing fiber material is arranged in the molding space of the mold, the fiber material is hermetically encapsulated with a bag film, a matrix resin is injected into the fiber material, and the bag film is depressurized, In a vacuum injection molding method for molding fiber reinforced plastic,
Opening one surface of the molding space;
Arranging a reinforcing fiber material in the mold,
To distribution in the porous film having a large number of small holes on the surface of the fibrous material,
Arranging a degassing sheet having a degassing circuit on the surface side of the porous film;
Arranging the bag film on the surface side of the degassing sheet so that the molding space is hermetically sealed;
The molding space is kept under reduced pressure via the degassing sheet by an external pressure source, and the resin viscosity at the time of resin injection is 20 Poise or less at the bottom of the fiber material in the molding space under reduced pressure. Injecting matrix resin,
A method for forming a fiber-reinforced plastic molded article comprising:
前記シート状強化繊維材料が多層であることを含んでなる請求項5記載の成形方法。The molding method according to claim 5, wherein the sheet-like reinforcing fiber material is a multilayer. バッグフィルムの周縁を成形型にシール材を介して気密に固定すること、
を含んでなる請求項5または6に記載の成形方法。
Be secured airtightly periphery of the bag film through the sealing material into the mold,
The shaping | molding method of Claim 5 or 6 which comprises these.
シート状の強化繊維材料の間にコア材を配することを含んでなることを特徴とする請求項7記載の成形方法。The molding method according to claim 7 , comprising disposing a core material between the sheet-like reinforcing fiber materials.
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