JPS6412206B2 - - Google Patents
Info
- Publication number
- JPS6412206B2 JPS6412206B2 JP56170217A JP17021781A JPS6412206B2 JP S6412206 B2 JPS6412206 B2 JP S6412206B2 JP 56170217 A JP56170217 A JP 56170217A JP 17021781 A JP17021781 A JP 17021781A JP S6412206 B2 JPS6412206 B2 JP S6412206B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- sheet
- carbon fiber
- prepreg
- matrix
- 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.)
- Expired
Links
- 229920005989 resin Polymers 0.000 claims description 52
- 239000011347 resin Substances 0.000 claims description 52
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 31
- 239000004917 carbon fiber Substances 0.000 claims description 31
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 20
- 239000011159 matrix material Substances 0.000 claims description 15
- 239000002904 solvent Substances 0.000 claims description 13
- 229920005992 thermoplastic resin Polymers 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 21
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 6
- 239000000835 fiber Substances 0.000 description 6
- 239000002131 composite material Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000004804 winding Methods 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000004793 Polystyrene Substances 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 229920002223 polystyrene Polymers 0.000 description 3
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical group ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000004696 Poly ether ether ketone Substances 0.000 description 2
- 239000004952 Polyamide Substances 0.000 description 2
- 239000004695 Polyether sulfone Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229920002492 poly(sulfone) Polymers 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- 229920000515 polycarbonate Polymers 0.000 description 2
- 229920006393 polyether sulfone Polymers 0.000 description 2
- 229920002530 polyetherether ketone Polymers 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920000193 polymethacrylate Polymers 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 235000019445 benzyl alcohol Nutrition 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000003562 lightweight material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229920005668 polycarbonate resin Polymers 0.000 description 1
- 239000004431 polycarbonate resin Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 239000012783 reinforcing fiber Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229950011008 tetrachloroethylene Drugs 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B15/00—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00
- B29B15/08—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00 of reinforcements or fillers
- B29B15/10—Coating or impregnating independently of the moulding or shaping step
- B29B15/12—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length
- B29B15/122—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length with a matrix in liquid form, e.g. as melt, solution or latex
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B15/00—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00
- B29B15/08—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00 of reinforcements or fillers
- B29B15/10—Coating or impregnating independently of the moulding or shaping step
- B29B15/12—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length
- B29B15/122—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length with a matrix in liquid form, e.g. as melt, solution or latex
- B29B15/125—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length with a matrix in liquid form, e.g. as melt, solution or latex by dipping
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Reinforced Plastic Materials (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
【発明の詳細な説明】
本発明はほぼ一方向に平行して拡開されたシー
ト状連続炭素繊維集合体を、溶剤に溶解した樹脂
液に含浸したあと、該炭素繊維を前記溶解樹脂と
同質のマトリツクス熱可塑性樹脂シートに貼着せ
しめ、繊維と樹脂とを貼着一体化したプリプレグ
の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention involves impregnating a sheet-like continuous carbon fiber aggregate spread in parallel in one direction with a resin solution dissolved in a solvent, and then impregnating the carbon fibers with the same material as the dissolved resin. The present invention relates to a method for manufacturing a prepreg in which fibers and resin are bonded together by bonding the prepreg to a matrix thermoplastic resin sheet.
従来、連続炭素繊維集合体には熱硬化性マトリ
ツクス樹脂のモノマーあるいは低重合物を含浸し
てプリプレグを製造し、これを硬化せしめた複合
成形品が知られているが、この場合、樹脂および
重合触媒を含浸せしめ、所定の形状に賦型したあ
と、樹脂を重合、架橋反応によつて硬化する必要
があるため、成形に長時間を要し、生産性が悪い
という欠点がある。また、含浸した樹脂および重
合触媒が経時的に変化し、複合成形品の機械的物
性の低下、成形性の低下が生じるため、プリプレ
グの保管状態を厳密に管理しなければならないと
いう問題点がある。 Conventionally, composite molded products are known in which continuous carbon fiber aggregates are impregnated with thermosetting matrix resin monomers or low polymers to produce prepregs and then cured. After being impregnated with a catalyst and molded into a predetermined shape, it is necessary to cure the resin through polymerization and crosslinking reactions, which has the drawback of requiring a long time for molding and poor productivity. In addition, the impregnated resin and polymerization catalyst change over time, resulting in a decline in the mechanical properties and moldability of the composite molded product, so there is a problem in that the storage conditions of the prepreg must be strictly controlled. .
これに対して複合成形品のマトリツクスの対象
となる熱可塑性樹脂は高重合度で耐薬品性や耐熱
性が高いため、連続した炭素繊維集合体に対し
て、生産性良く、樹脂付着率を任意に調節し、し
かも均一かつ親和性良く付着せしめることは非常
に難しい。 On the other hand, thermoplastic resin, which is used as the matrix for composite molded products, has a high degree of polymerization and high chemical and heat resistance, so it can be used for continuous carbon fiber aggregates with good productivity and any resin adhesion rate. It is very difficult to control the adhesion and to make it adhere uniformly and with good affinity.
例えば、樹脂を溶剤に溶解して炭素繊維に含浸
付着せしめるには熱可塑性樹脂は溶剤に対して難
溶性もしくは不溶性のものが多く、良溶剤のある
樹脂でも溶解度が低く、任意の樹脂付着率が得ら
れない。また、樹脂を加熱溶融して炭素繊維に含
浸するには樹脂溶融粘度が非常に高いために生産
性よく、しかも均一に付着せしめることが難し
い。 For example, when dissolving a resin in a solvent and impregnating it onto carbon fibers, thermoplastic resins are often poorly soluble or insoluble in solvents, and even resins with good solvents have low solubility, and a given resin adhesion rate is low. I can't get it. In addition, since the melt viscosity of the resin is extremely high when heat-melting the resin and impregnating it into carbon fibers, it is difficult to achieve good productivity and uniform adhesion.
かかる上記の問題点を解決するために本発明は
生産性が良くて、経時変化のない、しかも樹脂付
着率を任意に調節することが可能な、炭素繊維と
マトリツクスとが強固に結合しうる軽量にして高
性能を有する複合成形品のプリプレグを製造する
方法につき鋭意検討した結果、本発明に到達した
ものである。その要旨は連続炭素繊維集合体を拡
開装置によつて拡開したあと、後記マトリツクス
樹脂シートと同一の樹脂を溶剤に溶解した低粘度
の樹脂液に該炭素繊維を含浸し、繊維表面に樹脂
を浸透せしめ、これによつて繊維と樹脂との接触
界面の親和性を向上せしめ、
次いで、マトリツクス樹脂の付着率を調節する
ために前記樹脂液に含浸した炭素繊維を捲取りロ
ーラーで引取りながら、炭素繊維に付着した樹脂
の溶剤液が未乾燥の状態で、同方向に走行する熱
可塑性樹脂シートに連続的に接触することによつ
て該シート状連続炭素繊維集合体が樹脂シート面
に均一に貼着一体化された一方向プリプレグが得
られる。 In order to solve the above-mentioned problems, the present invention has developed a lightweight material that has good productivity, does not change over time, allows the resin adhesion rate to be arbitrarily adjusted, and can firmly bond carbon fiber and matrix. The present invention was arrived at as a result of intensive study on a method for manufacturing a prepreg composite molded article with high performance. The gist is that after a continuous carbon fiber aggregate is expanded using an expansion device, the carbon fibers are impregnated with a low-viscosity resin solution made by dissolving the same resin as the matrix resin sheet described later in a solvent, and the fiber surface is coated with resin. The carbon fibers impregnated with the resin liquid are then taken up with a winding roller to adjust the adhesion rate of the matrix resin. When the resin solvent solution adhering to the carbon fibers is not dried, it is brought into continuous contact with a thermoplastic resin sheet running in the same direction, so that the sheet-like continuous carbon fiber aggregate is uniformly distributed on the surface of the resin sheet. A unidirectional prepreg is obtained which is integrated with the unidirectional prepreg.
該プリプレグを必要枚数積層して加熱成形する
ことによつて溶融樹脂が炭素繊維間へ迅速に流動
し、短時間にして高性能の複合成形品を得ること
が可能であり、車輌、航空機等の構造材、電機電
子部品、スポーツ用品、工作機械部品等多方面に
亘り、適用しうる。 By laminating the required number of prepregs and heat-molding them, the molten resin quickly flows between the carbon fibers, making it possible to obtain high-performance composite molded products in a short time. It can be applied to a variety of fields such as structural materials, electrical and electronic parts, sporting goods, and machine tool parts.
本発明に用いられる熱可塑性マトリツクス樹脂
として具体的にはポリスルホン、ポリエーテルス
ルホン、ポリカーボネート、ポリスチレン、ポリ
メタクリレート、ポリアミド、ポリエーテルエー
テルケトン、ポリエチレン等でありこれらの樹脂
の分子構造的改質タイプあるいは結晶構造的改良
タイプ等も適用することができる。尚本発明でマ
トリツクス樹脂と同一の熱可塑性樹脂とは、共重
合成分や重合度等が相違することは差支えない。 Specific examples of the thermoplastic matrix resin used in the present invention include polysulfone, polyethersulfone, polycarbonate, polystyrene, polymethacrylate, polyamide, polyetheretherketone, polyethylene, etc., and molecularly modified types or crystals of these resins. Structural improvement types etc. can also be applied. In the present invention, the same thermoplastic resin as the matrix resin may be different in copolymerization components, degree of polymerization, etc.
溶剤としては例えばポリスルホンにはメチレン
クロライド、トリクロロエチレン、テトラクロロ
エチレン等の塩素化炭素水素や、シクロヘキサン
等、ポリエーテルスルホンにはメチレンクロライ
ド、トリクロロエチレン等の塩素化炭化水素やア
セトン、メチルエチルケトン等のケトン類、ポリ
カーボネートにはメチレンクロライド、ジクロル
エチレン等塩素化炭化水素およびジオキサン、テ
トラヒドロフラン等、ポリスチレンにはメチレン
クロライド、ジクロロエチレン等の塩素化炭化水
素およびトルエン、キシレン等の芳香族炭化水
素、ポリメタクリレートにはメチレンクロライド
等の塩素化炭化水素およびベンゼン等の芳香族炭
化水素、ポリアミドにはメタノール、エタノー
ル、エチレングリコール、ベンジルアルコール等
のアルコール類、ポリエチレンにはメチレンクロ
ライド等の塩素化炭化水素、ポリエーテルエーテ
ルケトンに対しては硫酸等があげられ、これらの
溶剤は単独の場合以外に混合して用いることや常
温以外に加熱して溶解度を向上せしめて用いるこ
とがある。 Examples of solvents include chlorinated hydrocarbons such as methylene chloride, trichlorethylene, and tetrachloroethylene, and cyclohexane for polysulfone; chlorinated hydrocarbons such as methylene chloride and trichloroethylene; and ketones such as acetone and methyl ethyl ketone for polyether sulfone; For polystyrene, chlorinated hydrocarbons such as methylene chloride, dichloroethylene, dioxane, tetrahydrofuran, etc., for polystyrene, chlorinated hydrocarbons such as methylene chloride, dichloroethylene, and aromatic hydrocarbons such as toluene and xylene, for polymethacrylate, such as methylene chloride, etc. Chlorinated hydrocarbons and aromatic hydrocarbons such as benzene; alcohols such as methanol, ethanol, ethylene glycol, and benzyl alcohol for polyamide; chlorinated hydrocarbons such as methylene chloride for polyethylene; and polyether ether ketone Examples include sulfuric acid, and these solvents may be used not only alone but also in combination, or heated to a temperature other than room temperature to improve solubility.
以下図面に従つて本発明の方法を詳細に説明す
る。第1図は本発明の方法を実施する場合の装置
の一例を側面図で示すものである。 The method of the present invention will be explained in detail below with reference to the drawings. FIG. 1 shows a side view of an example of an apparatus for carrying out the method of the present invention.
複数本の連続炭素繊維束1はガイドロール2を
経て拡開ロール37本によつて張力をかけられな
がら拡開されることによつて、ほぼ一方向に平行
で互に接したシート状連続炭素繊維集合体4にな
る。次いでこのシート状炭素繊維集合体は一定速
度で回転する繊維供給ロール対5を経て、溶剤で
溶解した樹脂液の入つた浸漬槽6に浸漬され、樹
脂が含浸される。 The plurality of continuous carbon fiber bundles 1 pass through a guide roll 2 and are spread out under tension by 37 spreader rolls, thereby forming continuous carbon sheets that are parallel to each other in almost one direction and in contact with each other. This becomes a fiber aggregate 4. Next, this sheet-like carbon fiber aggregate passes through a pair of fiber supply rolls 5 that rotate at a constant speed, and is immersed in a dipping tank 6 containing a resin solution dissolved in a solvent to be impregnated with resin.
樹脂が含浸したシート状炭素繊維集合体はニツ
プロール7を経て樹脂の溶剤液が未乾燥状態で、
1本もしくは対となつたマトリツクス樹脂シート
ロール8から樹脂シート供給ロール対9によつて
連続的に供給される樹脂シートに貼着ロール対1
0によつてシート表面に貼着されて、均一にして
一体化された一方向プリプレグとなり、プリプレ
グ巻取りロール11に捲取られる。 The sheet-like carbon fiber aggregate impregnated with resin passes through Nipprol 7, where the resin solvent solution is in an undried state.
A pair of adhering rolls 1 is applied to a resin sheet that is continuously supplied from one or a pair of matrix resin sheet rolls 8 by a pair of resin sheet supply rolls 9.
0 to the sheet surface to form a uniform and integrated unidirectional prepreg, which is then wound up onto a prepreg winding roll 11.
以上に説明した如く、本発明によれば樹脂付着
率を任意に調節することが可能であり炭素繊維と
マトリツクス樹脂とが強固に結合したプリプレグ
を連続的に生産性よく製造することが可能であ
る。 As explained above, according to the present invention, it is possible to arbitrarily adjust the resin adhesion rate, and it is possible to continuously and efficiently manufacture prepreg in which carbon fibers and matrix resin are firmly bonded. .
樹脂の溶剤液の粘度は100センチポイズ以下の
低粘度のものが通常用いられるが、炭素繊維表面
への均一付着性および繊維の集束性から10〜50セ
ンチポイズが好しい。 A low viscosity of 100 centipoise or less is usually used as the viscosity of the resin solvent solution, but 10 to 50 centipoise is preferable from the viewpoint of uniform adhesion to the carbon fiber surface and fiber cohesiveness.
樹脂付着率はシート状炭素繊維集合体と樹脂シ
ートの厚みをそれぞれ変えて、これらの組合せに
よつて調節することが可能である。樹脂シートは
厚み0.05〜0.3mmのものが主に用いられるが、炭
素繊維との重量割合によつては0.05mm以下もしく
は0.3mm以上の厚みのシートを使用することも可
能である。 The resin adhesion rate can be adjusted by changing the thicknesses of the sheet-like carbon fiber aggregate and the resin sheet, respectively, and by a combination of these. Resin sheets with a thickness of 0.05 to 0.3 mm are mainly used, but depending on the weight ratio with carbon fibers, sheets with a thickness of 0.05 mm or less or 0.3 mm or more can also be used.
シート状連続炭素繊維集合体と樹脂シートとの
貼着一体化は第2図に示すように樹脂シートの片
面に該炭素繊維を貼着せしめるケースと第3図に
示すように樹脂シートの間に該炭素繊維を貼着せ
しめるケースとがあり、炭素繊維の割合が特に高
い場合は前者の方が、一方樹脂の割合が特に高い
場合は後者の方が調整が容易である。 The bonding and integration of the sheet-like continuous carbon fiber aggregate and the resin sheet is achieved by attaching the carbon fibers to one side of the resin sheet as shown in Figure 2, and between the resin sheets as shown in Figure 3. There are cases in which the carbon fibers are attached, and the former is easier to adjust when the proportion of carbon fiber is particularly high, while the latter is easier to adjust when the proportion of resin is particularly high.
実施例
ポリカーボネート樹脂を塩化メチレンに溶解し
て、樹脂溶解度2.5重量%(溶液粘度約20センチ
ポイズ)の溶液を調整し、浸漬槽に注入した。こ
の樹脂液に連続炭素繊維束(フイラメント数
10000本)30本を拡開ロールによつて拡開せしめ、
ほぼ一方向に平行で、互に接したシート状連続炭
素繊維集合体に形成したあと含浸せしめ、ニツプ
ロールによつて樹脂付着率を約0.3%に調節した。
次いで該炭素繊維集合体は樹脂の溶剤液が未乾燥
のうちに、マトリツクス樹脂シートロール1本か
ら連続的に供給されるポリカーボネートシート
(厚み0.1mm)に貼着ロールによつてシート表面に
貼着されることにより、一体化された一方向プリ
プレグとなりプリプレグ巻取りロールに巻取つ
た。Example Polycarbonate resin was dissolved in methylene chloride to prepare a solution with a resin solubility of 2.5% by weight (solution viscosity of about 20 centipoise), and the solution was poured into a dipping tank. Continuous carbon fiber bundles (number of filaments) are added to this resin liquid.
10,000 pieces) Expand 30 pieces using an expansion roll,
After forming a sheet-like continuous carbon fiber aggregate that was parallel to one direction and in contact with each other, it was impregnated, and the resin adhesion rate was adjusted to about 0.3% using Nipprol.
Next, while the resin solvent solution is not dry, the carbon fiber aggregate is attached to the surface of the polycarbonate sheet (thickness 0.1 mm) continuously supplied from one matrix resin sheet roll using an attaching roll. As a result, an integrated unidirectional prepreg was formed and wound onto a prepreg winding roll.
かくして得られたプリプレグは厚み0.22m/m
目付280g/m2であつた。このプリプレグを縦110
mm、横210mmにカツトしたものを10枚積層して金
型に入れ、温度260℃、圧力14Kg/cm2で10分間プ
レスして平板を得た。該平板の性能は炭素繊維含
有率60重量%、引張強度148Kg/mm2、引張弾性率
9100Kg/mm2、曲げ強度117Kg/mm2、曲げ弾性率
8400Kg/mm2、層間剪断強度8.0Kg/mm2であつた。 The prepreg thus obtained has a thickness of 0.22 m/m.
The basis weight was 280g/ m2 . This prepreg is 110mm long
10 sheets cut to 210 mm wide were laminated, placed in a mold, and pressed for 10 minutes at a temperature of 260° C. and a pressure of 14 kg/cm 2 to obtain a flat plate. The properties of the flat plate are carbon fiber content of 60% by weight, tensile strength of 148Kg/mm 2 , and tensile modulus.
9100Kg/mm 2 , bending strength 117Kg/mm 2 , bending modulus
The interlaminar shear strength was 8,400 Kg/mm 2 and 8.0 Kg/mm 2 .
第1図は本発明の方法を実施する場合の装置の
一例を、第2図及び第3図は本発明のプリプレグ
シートの断面模式図である。
1……連続炭素繊維束、2……ガイドロール、
3……拡開ロール(7本)、4……シート状連続
炭素繊維集合体、5……繊維供給ロール対、6…
…浸漬槽、7……ニツプロール、8……マトリツ
クス樹脂シートロール1本もしくは対、9……樹
脂シート供給ロール対、10……貼着ロール、1
1……プリプレグ巻取ロール、12……補強用繊
維、13……マトリツクス樹脂フイルム層。
FIG. 1 shows an example of an apparatus for carrying out the method of the present invention, and FIGS. 2 and 3 are schematic cross-sectional views of the prepreg sheet of the present invention. 1... Continuous carbon fiber bundle, 2... Guide roll,
3... Expanding rolls (7 rolls), 4... Sheet-like continuous carbon fiber aggregate, 5... Fiber supply roll pair, 6...
...Immersion tank, 7...Nipro roll, 8...One matrix resin sheet roll or pair, 9...Resin sheet supply roll pair, 10...Packing roll, 1
1... Prepreg winding roll, 12... Reinforcing fiber, 13... Matrix resin film layer.
Claims (1)
続炭素繊維集合体にマトリツクス樹脂と同一の熱
可塑性樹脂の溶剤液を含浸付着せしめ、次いで、
未乾燥状態でマトリツクス樹脂となるシート状熱
可塑性樹脂と貼着一体化することを特徴とするプ
リプレグの製造方法。1. A sheet-like continuous carbon fiber aggregate spread in parallel to one direction is impregnated with a solvent solution of the same thermoplastic resin as the matrix resin, and then
A method for producing prepreg, which is characterized in that it is bonded and integrated with a sheet-like thermoplastic resin that becomes a matrix resin in an undried state.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56170217A JPS5871123A (en) | 1981-10-26 | 1981-10-26 | Prepreg manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56170217A JPS5871123A (en) | 1981-10-26 | 1981-10-26 | Prepreg manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5871123A JPS5871123A (en) | 1983-04-27 |
| JPS6412206B2 true JPS6412206B2 (en) | 1989-02-28 |
Family
ID=15900834
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56170217A Granted JPS5871123A (en) | 1981-10-26 | 1981-10-26 | Prepreg manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5871123A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS641524A (en) * | 1987-06-25 | 1989-01-05 | Asahi Glass Co Ltd | Preparation of fiber reinforced resin tape |
| EP3842203B1 (en) * | 2018-08-22 | 2024-02-14 | Toray Industries, Inc. | Production method for prepreg, prepreg tape, and fiber reinforced composite material, and coating device |
| WO2022054928A1 (en) * | 2020-09-11 | 2022-03-17 | 昭和電工マテリアルズ株式会社 | Method for producing frp precursor |
-
1981
- 1981-10-26 JP JP56170217A patent/JPS5871123A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5871123A (en) | 1983-04-27 |
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