JP2013049795A - Long carbon fiber reinforced polypropylene molded product - Google Patents

Long carbon fiber reinforced polypropylene molded product Download PDF

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JP2013049795A
JP2013049795A JP2011188912A JP2011188912A JP2013049795A JP 2013049795 A JP2013049795 A JP 2013049795A JP 2011188912 A JP2011188912 A JP 2011188912A JP 2011188912 A JP2011188912 A JP 2011188912A JP 2013049795 A JP2013049795 A JP 2013049795A
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polypropylene
carbon fiber
fiber reinforced
reinforced polypropylene
molded product
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JP5891657B2 (en
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Nori Yoshihara
法 葭原
Kohei Kiriyama
晃平 霧山
Hidenori Sugihara
秀紀 杉原
Satoshi Nago
聡 名合
Shoji Tsujii
彰司 辻井
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Toyobo Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To obtain a prepreg molded product for structural material with high flexural strength and thermal deformation resistance.SOLUTION: The long carbon fiber reinforced polypropylene molded products is obtained by molding long carbon fibre reinforced polypropylene containing 40-75 mass% of long carbon fiber and 25-60 mass% of polypropylene having two or more heat absorption peaks between 150-170°C in a heat flow curve of a differential scanning calorimeter.

Description

本発明は、炭素長繊維とポリプロピレン樹脂からなる成形品に関する。詳しくは、炭素長繊維と、高耐熱で、かつ高結晶化したポリプロピレン樹脂からなる成形品に関する。更に詳しくは、耐熱変形性と強度が著しく改善された構造材用成形品に関する。     The present invention relates to a molded article comprising carbon long fibers and polypropylene resin. Specifically, the present invention relates to a molded article made of a long carbon fiber and a highly heat-resistant and highly crystallized polypropylene resin. More specifically, the present invention relates to a molded article for a structural material having significantly improved heat distortion resistance and strength.

従来、ガラス長繊維強化ポリプロピレン複合材料は知られていた(例えば、文献1参照)。しかし、かかる従来技術は、ガラス繊維とポリプロピレンの接着性が低く、またガラス繊維の強度や弾性率への補強効果が低く、構造材としての実用性能は不満足であった。
ガラス繊維とポリプロピレンの接着性については、プロピレンを無水マレイン酸のような極性官能基により変性することは有効であると特開平05−001184(特許文献1)や特開平06−279615(特許文献2)に開示されている。さらに特殊なカップリング剤を含む集束剤で処理したガラス繊維を使用することが特開2005−170691(特許文献3)に開示されている。しかし、保安部品のような高強度の構造部材に要求される高い強度や物性の信頼性にははるかに未達であった。また、ガラス繊維より、強度や弾性率の高い炭素繊維を使用した炭素繊維強化ポリプロピレンについても、無水マレイン酸変性ポリオレフィン共重合体を使用して接着性を改善した組成物が特開2005−256206(特許文献4)に開示されている。しかし、炭素繊維とポリプロピレンの接着性はまだ低く、炭素繊維の高強度が複合材料に反映されず、構造材としての要求には未達であった。
Conventionally, a long glass fiber reinforced polypropylene composite material has been known (for example, see Document 1). However, such conventional technology has low adhesiveness between glass fiber and polypropylene, and has a low reinforcing effect on the strength and elastic modulus of glass fiber, and is unsatisfactory in practical performance as a structural material.
Regarding the adhesion between glass fiber and polypropylene, it is effective to modify propylene with a polar functional group such as maleic anhydride, as disclosed in JP-A Nos. 05-001184 (Patent Document 1) and JP-A No. 06-279615 (Patent Document 2). ). Furthermore, JP 2005-170691 (Patent Document 3) discloses the use of glass fibers treated with a sizing agent containing a special coupling agent. However, the reliability of the high strength and physical properties required for a high-strength structural member such as a safety part has not been achieved. Further, regarding carbon fiber reinforced polypropylene using carbon fiber having higher strength and elastic modulus than glass fiber, a composition having improved adhesiveness using a maleic anhydride-modified polyolefin copolymer is disclosed in JP-A-2005-256206 ( It is disclosed in Patent Document 4). However, the adhesion between the carbon fiber and the polypropylene is still low, and the high strength of the carbon fiber is not reflected in the composite material, and the demand as a structural material has not been achieved.

また、電線被覆法を応用したガラス長繊維強化ポリプロピレン樹脂複合材料は知られていた。しかし、かかる従来技術は、ガラス繊維とポリプロピレン樹脂のコンパウンド材料を主に射出成形により成形品を得ていた。コンパウンド工程や射出成形工程でガラス繊維の折損が著しく、ガラス繊維の強度や弾性率への補強効果が低下し、構造材としての実用性能には不満足であった。     Further, a long glass fiber reinforced polypropylene resin composite material using an electric wire coating method has been known. However, such a conventional technique obtains a molded product mainly by injection molding of a compound material of glass fiber and polypropylene resin. In the compounding process and injection molding process, breakage of the glass fiber was remarkable, the reinforcing effect on the strength and elastic modulus of the glass fiber was lowered, and the practical performance as a structural material was not satisfactory.

高強度・高剛性成形品を得るために、炭素長繊維とポリプロピレン樹脂の複合材料も研究開発された。しかし、射出成形や押出成形工程で炭素繊維が折損し、その効果は要求に大幅に未達であった。また、強化繊維の折損を避けるために、成形時のせん断変形の小さい圧縮成形についても検討された。しかし、強化繊維が長くなると繊維のからみ合いが起こり、流動性が著しく低下して、大型成形品や細いリブやボス構造を有する成形品は、欠肉が起こり良好な成形品が得られなかった。 In order to obtain high-strength and high-rigidity molded products, composite materials of carbon long fibers and polypropylene resin were also researched and developed. However, the carbon fiber was broken in the injection molding and extrusion molding processes, and the effect was not fully met. In order to avoid breakage of the reinforcing fiber, compression molding with small shear deformation at the time of molding was also examined. However, when the reinforcing fiber becomes longer, the fibers are entangled and the fluidity is remarkably lowered, and a large molded product or a molded product having a thin rib or boss structure is thinned and a good molded product cannot be obtained. .

繊維の絡み合いが起こらないように、繊維のロービングを単繊維状に開繊した後、ポリプロピレン樹脂を含浸して、強化繊維とポリプロピレン樹脂からなる一軸のテープ状プリプレグを予備成形した後、加熱圧縮成形する方法も開示された。炭素長繊維強化により、引張強度は改善されたが、引っ張りモード圧縮モードが複合される曲げ変形を受けた場合、曲げ強度の改善効果は、引っ張り強度に比較してかなり低く、曲げ変形を受ける構造材の強度要求には未達であった。曲げ強度は、炭素長繊維の分率を上げても必ずしも改善されず、ある分率を境に逆に低下し、炭素長繊維の分率を上げても要求を達成出来なかった。 To prevent fiber entanglement, fiber roving is opened into a single fiber, then impregnated with polypropylene resin, uniaxial tape-shaped prepreg made of reinforcing fiber and polypropylene resin is pre-formed, and then heat compression molded A method of doing so has also been disclosed. Although the tensile strength was improved by carbon long fiber reinforcement, the bending strength improvement effect is considerably lower than the tensile strength when subjected to bending deformation in which tensile mode compression mode is combined. The strength requirement of the material was not achieved. The bending strength was not necessarily improved even when the fraction of carbon long fibers was increased, but decreased on the contrary at a certain fraction, and the demand could not be achieved even when the fraction of carbon long fibers was increased.

一方、非特許文献2に開示されているように、ポリプロピレンの結晶化挙動の研究から結晶化温度を高くすると、完全度の高い結晶分率が高くなることは知られている。しかし、非特許文献3に開示されているように、ポリプロピレンを成形する場合の金型温度は、通常50〜80℃程度、強化繊維分率が極めて高い複合材料においても100〜120℃が選択される。120℃を超える融点近傍の金型温度での成形を、ポリプロピレンの成形過程で実行することは、結晶化速度はたいへん遅く、固化がなかなか進まず、現実不可能であった。従って、融点近傍の高い金型温度で成形した成形品は、どのような物性を示すか、取り分け強化繊維と複合系でどのような物性を示すかは全く不明であった。しかし、本発明者らは、結晶化速度を改善したポリプロピレン樹脂組成物を、炭素長繊維の繊維分率を高度にした強化複合体とすることにより、金型温度を通常の成形不良温度域をさらに超えた135℃以上の領域まで高めた成形においても脱型が可能であることを見出した。従来、成形出来無かった高温型による成形が可能になった。この技術を基に、これまで未知であった結晶化制御による物性改善の可能性が出てきた。 On the other hand, as disclosed in Non-Patent Document 2, it is known from the study of the crystallization behavior of polypropylene that when the crystallization temperature is increased, the crystal fraction with high completeness is increased. However, as disclosed in Non-Patent Document 3, the mold temperature for molding polypropylene is usually about 50 to 80 ° C., and 100 to 120 ° C. is selected even in a composite material having a very high reinforcing fiber fraction. The It was impossible to carry out molding at a mold temperature in the vicinity of the melting point exceeding 120 ° C. in the polypropylene molding process because the crystallization rate was very slow and solidification did not progress easily. Therefore, it has been completely unknown what kind of physical properties a molded product molded at a high mold temperature in the vicinity of the melting point, and especially what physical properties are exhibited in the reinforcing fiber and the composite system. However, the present inventors have made the mold resin temperature within the normal defective molding temperature range by making the polypropylene resin composition with improved crystallization speed into a reinforced composite with a high fiber fraction of carbon long fibers. Further, it was found that demolding is possible even in the molding which is increased to a temperature exceeding 135 ° C. Molding with a high temperature mold that could not be molded in the past has become possible. Based on this technology, the possibility of improving physical properties by crystallization control, which has been unknown up to now, has emerged.

特開平05−001184号公報Japanese Patent Laid-Open No. 05-001184 特開平06−279615号公報Japanese Patent Laid-Open No. 06-279615 特開2005−170691号公報JP 2005-170691 A 特開2005−256206号公報JP-A-2005-256206

プラスチックス、Vol.36(7),p103(1985)Plastics, Vol. 36 (7), p103 (1985) Polymer Journal, Vol.5, p111 (1973)Polymer Journal, Vol. 5, p111 (1973) 新版 複合材料・技術総覧 p351, 産業技術サービスセンター,(2011)New edition Composite material and technology overview p351, Industrial Technology Service Center, (2011) Polymer, vol.36 No.12, p2407 (1995)Polymer, vol.36 No.12, p2407 (1995) Crystallization of Polymers Second Edition vol.1, p265 Cambridge University Press (2002)Crystallization of Polymers Second Edition vol.1, p265 Cambridge University Press (2002)

構造材の場合、高い強度や高い耐熱変形性が必要な部品が多い。強化ポリプロピレンの高強度化や高耐熱化ができれば、構造材用途へのポリプロピレン複合材料の適用範囲が拡大することから、強化ポリプロピレンの結晶化制御による高強度化および高耐熱化の市場の高い開発要求があった。
本発明は、かかる従来技術の課題を背景になされたものである。すなわち、本発明の目的は、ポリプロピレンの結晶化を制御して得られた強度や耐熱性が飛躍的に優れた比強度の高い構造材用ポリプロピレン複合材成形品を提供することにある。
In the case of structural materials, there are many parts that require high strength and high heat distortion resistance. If the strength and heat resistance of reinforced polypropylene can be increased, the range of application of polypropylene composite materials for structural materials will increase. Therefore, there is a high development demand in the market for high strength and high heat resistance by controlling the crystallization of reinforced polypropylene. was there.
The present invention has been made against the background of such prior art problems. That is, an object of the present invention is to provide a polypropylene composite material molded article for a structural material having a high specific strength and dramatically improved strength and heat resistance obtained by controlling crystallization of polypropylene.

本発明者らは鋭意検討した結果、以下に示す手段により、上記課題を解決できることを見出し、本発明に到達した。
すなわち、本発明は、以下の構成からなる。
1.炭素長繊維を40〜75質量%含有し、示差走査熱量計のヒートフロー曲線が150℃〜170℃の間に2つ以上の吸熱ピークもつポリプロピレンを25〜60質量%含有する炭素長繊維強化ポリプロピレンを成形してなることを特徴とする炭素長繊維強化ポリプロピレン成形品。
2.前記ポリプロピレンが、150℃〜170℃の間のヒートフロー曲線の吸熱ピークの中で、最も高い吸熱値を示す吸熱ピークの吸熱値に対して2番目に高い吸熱値を示す吸熱ピークの吸熱値がその60%以上であることを特徴とする1.に記載の炭素長繊維強化ポリプロピレン成形品。
3.樹脂成分1g当たりの融解熱が、97J以上であることを特徴とする1.に記載の炭素長繊維強化ポリプロピレン成形品。
4.成形部分の表面温度が135℃以上である金型を使用して圧縮成形されたことを特徴とする1.〜3.のいずれかに記載の炭素長繊維強化ポリプロピレン成形品。
As a result of intensive studies, the present inventors have found that the above problems can be solved by the following means, and have reached the present invention.
That is, this invention consists of the following structures.
1. Carbon long fiber reinforced polypropylene containing 40 to 75% by mass of carbon long fiber and 25 to 60% by mass of polypropylene having two or more endothermic peaks between 150 ° C. and 170 ° C. in the heat flow curve of the differential scanning calorimeter A carbon long fiber reinforced polypropylene molded product characterized by being molded.
2. In the endothermic peak of the heat flow curve between 150 ° C. and 170 ° C., the endothermic value of the endothermic peak showing the second highest endothermic value with respect to the endothermic value of the endothermic peak showing the highest endothermic value is obtained. It is characterized by being 60% or more. The long carbon fiber reinforced polypropylene molded product described in 1.
3. 1. Heat of fusion per gram of resin component is 97 J or more The long carbon fiber reinforced polypropylene molded product described in 1.
4). 1. The molding part is compression-molded using a mold having a surface temperature of 135 ° C. or higher. ~ 3. A carbon long fiber reinforced polypropylene molded article according to any one of the above.

複合材料の母相の結晶性を制御した本発明により、曲げ強度や荷重たわみ温度が飛躍的に高くなり、設計の自由度が増し、構造材の軽薄短小化への要求を満たす複合材料を工業的に提供することができる。本発明により得られた複合材料を成形して得られる成形品は、自動車のフレーム部品や機械器具の構造部材やスポーツ器具などに使用される。本発明により、高い曲げ強度を有する複合材料が提供される理由は、未だ明確でないが、この効果は、母相に特定の結晶を高度に発現することにより、母相の弾性率を改善することで、圧縮面の母相中の炭素繊維やこのコンポジットの座屈が防止されたことと、母相の高い収縮率により、炭素繊維の拘束力が増し、樹脂―炭素繊維間の接着力が増大し炭素繊維の高い引っ張り強度が有効に作用したものと考察される。   The present invention, which controls the crystallinity of the matrix of the composite material, dramatically increases the bending strength and the deflection temperature under load, increases the degree of design freedom, and industrializes composite materials that meet the demands for lighter, thinner and smaller structural materials. Can be provided. A molded product obtained by molding the composite material obtained by the present invention is used for a frame part of an automobile, a structural member of a mechanical instrument, a sports instrument, and the like. The reason why a composite material having high bending strength is provided by the present invention is not yet clear, but this effect improves the elastic modulus of the matrix by highly expressing specific crystals in the matrix. Because of the prevention of buckling of the carbon fiber and this composite in the matrix of the compression surface and the high shrinkage of the matrix, the binding force of the carbon fiber is increased and the adhesion between the resin and the carbon fiber is increased. It is considered that the high tensile strength of the carbon fiber worked effectively.

実施例のDSC測定によるヒートフロー図。150℃と170℃の間に吸熱のダブルピークを有し、実線で示した最も高い吸熱フローに対し点線で示した2番目に高い吸熱フローの比は0.97である。The heat flow figure by DSC measurement of an Example. The ratio of the second highest endothermic flow shown by the dotted line to the highest endothermic flow shown by the solid line is 0.97, with a double peak of endotherm between 150 ° C and 170 ° C. 実施例のDSC測定によるヒートフロー図。150℃と170℃の間にショルダー状に吸熱のダブルピークを有し、実線で示した最も高い吸熱フローに対し点線で示した2番目に高い吸熱フローの比は0.94である。The heat flow figure by DSC measurement of an Example. The shoulder has an endothermic double peak between 150 ° C. and 170 ° C., and the ratio of the second highest endothermic flow indicated by the dotted line to the highest endothermic flow indicated by the solid line is 0.94. 比較例のDSC測定によるヒートフロー図。150℃と170℃の間に吸熱ピークはひとつである。このヒートフローに対して0.6以上のショルダー状ヒートフローも検出されない。The heat flow figure by DSC measurement of a comparative example. There is one endothermic peak between 150 ° C and 170 ° C. A shoulder heat flow of 0.6 or more is not detected for this heat flow.

以下、本発明を詳述する。
1.炭素長繊維を40〜75質量%含有し、示差走査熱量計のヒートフロー曲線が150℃〜170℃の間に2つ以上の吸熱ピークもつポリプロピレンを25〜60質量%含有する炭素長繊維強化ポリプロピレンを成形してなることを特徴とする炭素長繊維強化ポリプロピレン成形品。
2.前記ポリプロピレンが、150℃〜170℃の間のヒートフロー曲線の吸熱ピークの中で、最も高い吸熱値を示す吸熱ピークの吸熱値に対して2番目に高い吸熱値を示す吸熱ピークの吸熱値がその60%以上であることを特徴とする1.に記載の炭素長繊維強化ポリプロピレン成形品。
3.樹脂成分1g当たりの融解熱が、97J以上であることを特徴とする1.に記載の炭素長繊維強化ポリプロピレン成形品。
4.成形部分の表面温度が135℃以上である金型を使用して圧縮成形されたことを特徴とする1.〜3.のいずれかに記載の炭素長繊維強化ポリプロピレン成形品。
The present invention is described in detail below.
1. Carbon long fiber reinforced polypropylene containing 40 to 75% by mass of carbon long fiber and 25 to 60% by mass of polypropylene having two or more endothermic peaks between 150 ° C. and 170 ° C. in the heat flow curve of the differential scanning calorimeter A carbon long fiber reinforced polypropylene molded product characterized by being molded.
2. In the endothermic peak of the heat flow curve between 150 ° C. and 170 ° C., the endothermic value of the endothermic peak showing the second highest endothermic value with respect to the endothermic value of the endothermic peak showing the highest endothermic value is obtained. It is characterized by being 60% or more. The long carbon fiber reinforced polypropylene molded product described in 1.
3. 1. Heat of fusion per gram of resin component is 97 J or more The long carbon fiber reinforced polypropylene molded product described in 1.
4). 1. The molding part is compression-molded using a mold having a surface temperature of 135 ° C. or higher. ~ 3. A carbon long fiber reinforced polypropylene molded article according to any one of the above.

本発明は、40質量%以上の炭素繊維とポリプロピレンの特殊な結晶構造の組み合わせにより得られる成形品である。一般的な成形条件下で発現する結晶は、α型の結晶形態が主で、ISO11357-3により測定される融点は、単一ピークである。非特許文献4によると、α型結晶の他に、結晶核剤の選択により発現することが知られているβ型や、圧縮下における結晶化で発現することが知られているγ型があるが、β型やγ型結晶は、α型結晶より融点が低く、高融点・高弾性率を目的とする本発明には適さない。これに対して、本発明の炭素繊維とポリプロピレンからなるプリプレグを、135℃を超える金型でスタンピング成形して得られた成形品中のポリプロピレンの融解は、150℃〜170℃間に多重のピークを示し、高温側のピーク温度は、135℃未満の金型で成形して得られた融点のピーク温度より1.5℃以上高い融点を示す。すなわち、高融点結晶の発現により、曲げ強さや耐熱変形性が向上することを示している。広角X線回折ポロファイルから推察される結晶形態は、α型が主で、これにγ型が混在している。本発明でいう母相がポリプロピレンからなることは、樹脂の熱分析における融点と広角X線回折によるプロファイルがポリプロピレンの特性と一致することであり、樹脂中のポリプロピレンは60質量%以上、好ましくは80質量%以上である。また本発明では、150℃と170℃間で最も高い吸熱ピーク値と2番目に高い吸熱ピーク値とベースライン間のそれぞれの高さを計測し、最も高い吸熱ピーク値に対する2番目に高い吸熱ピーク値の比率は0.6以上が好ましく、0.75以上が特に好ましい。前記比率が高いことは、融点の多重ピークを明確に示し、融解熱が高いことに関連するから好ましい。ピーク値の比率が0.6未満では、結晶化度が低く耐熱性や機械的性質が低くなり、本発明の目的を達成しない。
また本発明の成形品中のポリプロピレンの総結晶化度は、X線回折プロファイルからBragg反射の積分強度や示差走査熱量計(DSC)の融解エンタルピーと完全結晶の融解エンタルピーの比率から求めることができる。本発明の成形品に含まれるポリプロピレン総結晶化度は、46%以上が好ましく、特に50%以上が好ましい。非特許文献4によると、α型ポリプロピレンの完全結晶融解エンタルピーは、208.8J/gであり、樹脂成分当たり1g当たり、97J以上が好ましく、特に104.4Jであることが好ましい。97J未満では、弾性率、特に50℃以上の高温における弾性率が低く、機械的物性や耐熱性が低下するから好ましくない。
The present invention is a molded article obtained by combining a special crystal structure of 40% by mass or more of carbon fiber and polypropylene. Crystals developed under general molding conditions are mainly in the α-type crystal form, and the melting point measured by ISO11357-3 is a single peak. According to Non-Patent Document 4, in addition to α-type crystals, there are β-types that are known to be expressed by selection of crystal nucleating agents and γ-types that are known to be expressed by crystallization under compression. However, β-type and γ-type crystals have lower melting points than α-type crystals and are not suitable for the present invention aiming at a high melting point and a high elastic modulus. On the other hand, the melting of polypropylene in a molded product obtained by stamping the prepreg composed of the carbon fiber and polypropylene of the present invention with a mold exceeding 135 ° C has multiple peaks between 150 ° C and 170 ° C. The peak temperature on the high temperature side shows a melting point higher by 1.5 ° C. or more than the peak temperature of the melting point obtained by molding with a mold of less than 135 ° C. That is, it shows that the bending strength and the heat distortion resistance are improved by the development of the high melting point crystal. The crystal form inferred from the wide-angle X-ray diffraction porofile is mainly α-type, and γ-type is mixed therewith. The fact that the mother phase as used in the present invention is composed of polypropylene means that the melting point in the thermal analysis of the resin and the profile by wide-angle X-ray diffraction agree with the characteristics of polypropylene, and the polypropylene in the resin is 60% by mass or more, preferably 80%. It is at least mass%. In the present invention, the highest endothermic peak value between 150 ° C and 170 ° C, the second highest endothermic peak value, and the height between the baselines are measured, and the second highest endothermic peak with respect to the highest endothermic peak value. The value ratio is preferably 0.6 or more, particularly preferably 0.75 or more. A high ratio is preferred because it clearly shows multiple peaks of melting point and is related to a high heat of fusion. If the ratio of the peak values is less than 0.6, the degree of crystallinity is low, the heat resistance and mechanical properties are low, and the object of the present invention is not achieved.
The total crystallinity of polypropylene in the molded product of the present invention can be determined from the X-ray diffraction profile from the integrated intensity of Bragg reflection and the ratio of the melting enthalpy of the differential scanning calorimeter (DSC) to the melting enthalpy of the complete crystal. . The total crystallinity of polypropylene contained in the molded article of the present invention is preferably 46% or more, particularly preferably 50% or more. According to Non-Patent Document 4, the complete crystal melting enthalpy of α-type polypropylene is 208.8 J / g, preferably 97 J or more per 1 g of resin component, and particularly preferably 104.4 J. If it is less than 97 J, the elastic modulus, particularly the elastic modulus at a high temperature of 50 ° C. or higher is low, and the mechanical properties and heat resistance are deteriorated.

本発明に使用されるポリプロピレンは特に限定されないが、本発明に使用されるポリプロピレンとしては、プリプレグ作製時の含浸性から分岐構造が殆どなく、物性的には高い弾性率を有する、95モル%以上がプロピレン繰り返し単位からなるホモタイプのポリプロピレンで、アイソタクチックスの立体規則性分率の高いものが好ましい。また、本発明に使用されるポリプロピレンの重合触媒は、特に限定されないが、立体規則性や分子量分布がシャープなポリプロピレンが提供できるメタロセン系触媒が好ましい。 The polypropylene used in the present invention is not particularly limited, but the polypropylene used in the present invention has almost no branched structure due to impregnation properties during prepreg production, and has a high elastic modulus in terms of physical properties, 95 mol% or more. Is preferably a homo-type polypropylene composed of propylene repeating units and having a high stereotactic fraction of isotactics. In addition, the polymerization catalyst for polypropylene used in the present invention is not particularly limited, but a metallocene catalyst that can provide a polypropylene having a stereoregularity and a sharp molecular weight distribution is preferable.

炭素繊維との接着性の面から、炭素繊維と接着性を有する官能基が導入され変性されたポリプロピレンが本発明に好ましい。特に、接着性を有する官能基としては、酸基が好ましい。更に、本発明で好ましく使用される酸変性ポリプロピレンの重量平均分子量は、8万〜20万、好ましくは9万〜18万である。重量平均分子量が、20万を超えると、溶融粘度が高くなり、プリプレグ作製時、含浸性が低く、ボイドを含み易く、本発明が達成されない。また重量平均分子量が8万未満では、強度や伸度が低く、プリプレグから得られる成形品の強度・伸度が低く好ましくない。重合触媒としては、チグラーナッタ触媒より、メタロセン系触媒が好ましい。また酸変性は、有機過酸化物によるラジカルにより、不飽和酸や不飽和無水酸をグラフトすることで得られる。有機過酸化物では、パーオキシジカーボネート系やパーオキシケタール系より、ジアルキルパーオキサイドが好ましい。本発明に使用される酸変性ポリプロピレンの多分散性指数(数平均分子量に対する重量平均分子量の比)には1.5〜7、好ましくは1.6〜6、特に好ましくは1.7〜5である。多分散指数は、1.5未満の酸変性ポリプロピレンを得るには、分別処理が必要でコスト高となり、好ましくない。また7を超えると、重量平均分子量が、8万〜20万の範囲内あっても、混在する低分子量ポリプロピレンが強度・伸度を低下させるので好ましくない。逆に、混在する高分子量成分は、含浸性や接着性を低下させて好ましくない。多分散性指数が小さいために、比較的低い重量平均分子量品でも、低分子量成分が非常に少なく、酸変性ポリプロピレンの強伸度が高くなったためと考察される。プリプレグ製造時の含浸性は、重量平均分子量に強く依存する、一方機械的性質は低分量成分に依存することが分かった。分子量分布を大変狭く制御することで、低い重量平均分子量と少ない低分子量成分を両立することが可能となる。
重量平均分子量およびその分布は、JISK7252系に準じて、140℃の1,2,4−トリクロロベンゼン溶液について、ゲル浸透クロマトグラフィー法により、140℃の高温カラムを使用して測定される。
From the viewpoint of adhesiveness to carbon fibers, polypropylene modified by introducing functional groups having adhesiveness with carbon fibers is preferred in the present invention. In particular, an acid group is preferable as the functional group having adhesiveness. Furthermore, the weight average molecular weight of the acid-modified polypropylene preferably used in the present invention is 80,000 to 200,000, preferably 90,000 to 180,000. When the weight average molecular weight exceeds 200,000, the melt viscosity becomes high, and when the prepreg is produced, the impregnation property is low and voids are easily contained, and the present invention is not achieved. If the weight average molecular weight is less than 80,000, the strength and elongation are low, and the strength and elongation of the molded product obtained from the prepreg is low, which is not preferable. As a polymerization catalyst, a metallocene catalyst is preferable to a Ziegler-Natta catalyst. Acid modification can be obtained by grafting an unsaturated acid or an unsaturated acid anhydride with a radical derived from an organic peroxide. Of the organic peroxides, dialkyl peroxides are preferred to peroxydicarbonates and peroxyketals. The polydispersity index (ratio of the weight average molecular weight to the number average molecular weight) of the acid-modified polypropylene used in the present invention is 1.5 to 7, preferably 1.6 to 6, particularly preferably 1.7 to 5. is there. In order to obtain an acid-modified polypropylene having a polydispersity index of less than 1.5, a fractionation treatment is required, resulting in an increase in cost. On the other hand, when it exceeds 7, even if the weight average molecular weight is in the range of 80,000 to 200,000, the mixed low molecular weight polypropylene lowers the strength and elongation, which is not preferable. On the other hand, the mixed high molecular weight component is not preferable because it impregnates and impairs. Since the polydispersity index is small, it is considered that even in a relatively low weight average molecular weight product, the low molecular weight component is very small and the high elongation of acid-modified polypropylene is high. It was found that the impregnation properties during prepreg production depended strongly on the weight average molecular weight, while the mechanical properties depended on the low component. By controlling the molecular weight distribution very narrowly, it is possible to achieve both a low weight average molecular weight and a low low molecular weight component.
The weight average molecular weight and the distribution thereof are measured by a gel permeation chromatography method using a 140 ° C. high temperature column for a 1,2,4-trichlorobenzene solution at 140 ° C. according to JIS K7252.

本発明に使用される酸変性ポリプロピレンは、強化材と高い接着強度を有することが必要であり、赤外吸収スペルトルにおいて、840cm−1の吸光度面積に対して1790cm−1と1710cm−1の吸光度面積の和の比が0.1〜1.2、好ましくは0.2〜1.0である酸変性されている。無水酸変性度の尺度である吸光度面積の比が0.1未満では、プリプレグを成形して得られる成形品の強度が低く好ましくない。また1.2を超えると、熱分解や熱変色が起こり好ましくない。酸成分としては、マレイン酸、イタコン酸、コハク酸、アジピン酸などの無水酸やアクリル酸、メタクリル酸などが例示される。好ましくは、変性のしやすさからマレイン酸、イタコン酸の無水酸である。840cm−1は、ポリプロピレンに由来する赤外線吸収であり、測定した試験片の厚さ補正係数である。また1790cm−1,1710cm−1は、それぞれ無水カルボン酸とカルボン酸に由来する吸収であり、吸水と脱水状態を移行するから総合した変性度で効果は整理される。 Acid-modified polypropylene used in the present invention, it is necessary to have a reinforcement and high adhesive strength, in an infrared absorption Superutoru, absorbance area of 1790 cm -1 and 1710 cm -1 relative to the absorbance area of 840 cm -1 Is modified with an acid that has a ratio of 0.1 to 1.2, preferably 0.2 to 1.0. If the ratio of the absorbance area, which is a measure of the degree of acid anhydride modification, is less than 0.1, the strength of the molded product obtained by molding the prepreg is low, which is not preferable. On the other hand, if it exceeds 1.2, thermal decomposition and thermal discoloration occur, which is not preferable. Examples of the acid component include anhydrides such as maleic acid, itaconic acid, succinic acid, and adipic acid, acrylic acid, and methacrylic acid. Of these, maleic acid and itaconic acid anhydride are preferred because they are easily modified. 840 cm −1 is infrared absorption derived from polypropylene, and is a thickness correction coefficient of the measured test piece. In addition, 1790 cm −1 and 1710 cm −1 are absorptions derived from carboxylic anhydride and carboxylic acid, respectively, and the effects are arranged by the total degree of modification since the water absorption and dehydration states are transferred.

本発明の酸変性ポリプロピレン樹脂及び組成物は、出発原料や製造条件は制限されないが、メルトフローレート0.1〜4dg/minであるポリプロピレン100質量部に対して、無水マレイン酸0.01〜5質量部、半減期が1分となる温度が170〜185℃の範囲にある有機過酸化物0.05〜3質量部を溶融混練して得られることが好ましい態様である。半減期とは、有機過酸化物が熱分解して半分になるまでの時間であり、反応温度とラジカル反応に必要な時間の関係の指標となる。
ポリプロピレンに不飽和ジカルボン酸化合物と有機過酸化物を作用させて酸変性する方法が、工業的には好ましいが、この方法による変性時、ポリプロピレンの分子鎖はラジカルで切断される副反応が伴う。この反応を制御するには、有機過酸化物のラジカル発生特性が適合することが必要である。半減期が1分となる温度が170〜185℃、好ましくは、172〜183℃である有機過酸化物が好ましい。170℃未満では、低分子量のポリプロピレンのみ溶融した状態からラジカル発生を開始するから低分量のポリプロピレンが発生しやすく、多分散性指数が高くなり好ましくない。また185℃を超えると、滞留時間が2分以下の押出機で変性反応を行う場合、230℃以上の高温が必要となり、熱分解や熱変色を伴いやすく、品質安定性の面から好ましくない。半減期が1分となる温度が、170〜185℃である有機過酸化物としては、メチルエチルケトンパーオキシド(182℃)、t−ブチルハイドロパーオキシド(179℃)、ジクミルパーオキシド(172℃)、2,5ジメチル2,5ジ(t−ブチルパーオキシド)ヘキサン(180℃)、nーブチル4,4−ジ(t−ブチルパーオキシ)バレレート(173℃)などが例示される。これらの中では、t−ブチルハイドロパーオキシド(179℃)、ジクミルパーオキシド(172℃)、2,5ジメチル2,5ジ(t−ブチルパーオキシド)ヘキサン(180℃)が活性酸素量も高く好ましい。ポリプロピレン100質量部に対して、無水マレイン酸0.01〜5質量部をグラフト変性する場合、活性酸素の必要量から、有機過酸化物は0.05〜3質量部、好ましくは、0.1〜1質量部使用される。
0.05質量部未満では、反応不足となりやすく好ましくない。3質量部を超えると低分子量ポリプロピレンにもラジカルの作用が起こりやすく好ましくない。
The starting material and production conditions of the acid-modified polypropylene resin and composition of the present invention are not limited, but maleic anhydride is 0.01 to 5 with respect to 100 parts by mass of polypropylene having a melt flow rate of 0.1 to 4 dg / min. A preferred embodiment is obtained by melting and kneading 0.05 to 3 parts by mass of an organic peroxide having a mass part and a half-life of 1 minute in the range of 170 to 185 ° C. The half-life is the time until the organic peroxide is thermally decomposed and halved, and is an indicator of the relationship between the reaction temperature and the time required for the radical reaction.
A method of acid-modifying by reacting an unsaturated dicarboxylic acid compound and an organic peroxide on polypropylene is industrially preferable. However, at the time of modification by this method, the molecular chain of polypropylene is accompanied by a side reaction that is cleaved by radicals. To control this reaction, the radical generation characteristics of the organic peroxide must be matched. An organic peroxide having a half-life of 1 minute at 170 to 185 ° C, preferably 172 to 183 ° C is preferred. When the temperature is less than 170 ° C., radical generation starts from a state in which only a low molecular weight polypropylene is melted, so that a low amount of polypropylene is likely to be generated, and the polydispersity index becomes high. On the other hand, when the temperature exceeds 185 ° C., when the modification reaction is carried out with an extruder having a residence time of 2 minutes or less, a high temperature of 230 ° C. or more is required, which is likely to be accompanied by thermal decomposition and thermal discoloration, which is not preferable from the viewpoint of quality stability. Examples of the organic peroxide having a half-life of 1 minute at 170 to 185 ° C include methyl ethyl ketone peroxide (182 ° C), t-butyl hydroperoxide (179 ° C), and dicumyl peroxide (172 ° C). 2,5-dimethyl-2,5-di (t-butylperoxide) hexane (180 ° C.), n-butyl 4,4-di (t-butylperoxy) valerate (173 ° C.) and the like. Among these, t-butyl hydroperoxide (179 ° C.), dicumyl peroxide (172 ° C.), 2,5 dimethyl 2,5 di (t-butyl peroxide) hexane (180 ° C.) has an active oxygen content. Highly preferred. When 0.01 to 5 parts by mass of maleic anhydride is graft-modified with respect to 100 parts by mass of polypropylene, the organic peroxide is 0.05 to 3 parts by mass, preferably 0.1 ~ 1 part by mass is used.
If it is less than 0.05 parts by mass, the reaction tends to be insufficient, which is not preferable. When the amount exceeds 3 parts by mass, the low molecular weight polypropylene is not preferable because radical action is likely to occur.

本発明には、炭素長繊維や連続繊維が使用される。重量平均繊維長が10mm未満では、構造材としての強度が未達となり、好ましくない。機械物性上は連続繊維が好ましいが、成形時の金型内における流動性が必要なことからプリプレグとしてより短く切断されたものが使用されることもある。炭素繊維としては、製造法に特に制限されないが、ポリアクリロニトル繊維やセルロース繊維などの繊維を空気中で200〜300℃にて処理した後、不活性ガス中で1000〜3000℃以上で焼成され炭化製造された引張り強度20t/cm以上、引張り弾性率200GPa以上の炭素繊維が好ましい。本発明に使用される単繊維径は、特に制限されないが、複合化の製造ライン工程から3〜25μmが好ましく、特に4〜15μmが好ましい。3μm未満では、含浸や脱泡が難しく、25μmを超えると、比表面積が小さくなり、複合化の効果が小さくなり好ましくない。本発明に使用される炭素繊維は、空気や硝酸による湿式酸化、乾式酸化、ヒートクリーニング、ウイスカライジングなどによる接着性改良のための処理されたものが好ましい。また本発明の複合材料製造に使用される炭素繊維は、作業工程の取り扱い性から、100℃以下で軟化する集束剤により集束されていることが好ましい。集束フィラメント数には特に制限ないが、1000〜30000フィラメント、好ましくは、3000〜25000フィラメントが好ましい。本発明に使用される炭素繊維の集束剤は特に限定されないが、炭素繊維と母相のポリプロピレン樹脂に高い接着力を有するウレタン系やエポキシ系集束剤が好ましい。 In the present invention, carbon long fibers and continuous fibers are used. If the weight average fiber length is less than 10 mm, the strength as a structural material is not achieved, which is not preferable. In view of mechanical properties, continuous fibers are preferable, but since the fluidity in the mold at the time of molding is required, a prepreg that has been cut shorter may be used. Although it does not restrict | limit especially in a manufacturing method as carbon fiber, After processing fibers, such as a polyacrylonitrile fiber and a cellulose fiber, in air at 200-300 degreeC, it is baked at 1000-3000 degreeC or more in inert gas. Carbon fibers produced by carbonization and having a tensile strength of 20 t / cm 2 or more and a tensile modulus of 200 GPa or more are preferred. Although the diameter of the single fiber used in the present invention is not particularly limited, it is preferably 3 to 25 μm, particularly preferably 4 to 15 μm, from the production line process of the composite. If it is less than 3 μm, impregnation and defoaming are difficult, and if it exceeds 25 μm, the specific surface area becomes small and the effect of compositing becomes unfavorable. The carbon fiber used in the present invention is preferably treated for improving adhesion by wet oxidation with air or nitric acid, dry oxidation, heat cleaning, whiskerizing, or the like. Moreover, it is preferable that the carbon fiber used for composite material manufacture of this invention is bundled by the bundling agent which softens at 100 degrees C or less from the handleability of a work process. Although there is no restriction | limiting in particular in the number of focusing filaments, 1000-30000 filaments, Preferably 3000-25000 filaments are preferable. The carbon fiber sizing agent used in the present invention is not particularly limited, but a urethane-based or epoxy-based sizing agent having high adhesion to the carbon fiber and the polypropylene resin of the parent phase is preferable.

本発明の成形品には、40〜75質量%、好ましくは50〜70質量%、特に好ましくは55〜70質量%の炭素長繊維が複合される。40質量%未満では、炭素長繊維による補強の効果が不十分となり、また炭素長繊維を含有する上限は特に制限されないが、75質量%を超えると、炭素繊維へのポリプロピレン樹脂の含浸が困難であり、共に本発明の目的である構造部材としての要求を満たせず好ましくない。   40 to 75% by mass, preferably 50 to 70% by mass, particularly preferably 55 to 70% by mass of carbon long fibers are composited in the molded article of the present invention. If it is less than 40% by mass, the effect of reinforcing with carbon long fibers is insufficient, and the upper limit for containing carbon long fibers is not particularly limited, but if it exceeds 75% by mass, it is difficult to impregnate carbon fibers with polypropylene resin. Both are unfavorable because they do not satisfy the requirements of the structural member that is the object of the present invention.

本発明の成形品には、上記の必須成分の他に物性改良・成形性改良、耐久性改良を目的として、結晶核剤、滑剤、酸化防止剤、難燃剤、耐光剤、耐候剤などが配合できる。
本発明の複合材料の製造法は特に限定されない。例えば、ポリプロピレン樹脂の融点以上に温度調節されたスクリュータイプ押出機のホッパーにポリプロピレン樹脂および/またはポリプロピレン樹脂共重合体などを所定割合に予備混合して供給する。溶融樹脂をギアポンプの回転数にて計量して、樹脂の融点以上に温度調節された含浸用押出機の上流に供給する。一方、ロービング状炭素繊維を拡張開繊し、含浸用押出機の下流に供給する。下流先端に開口部を絞ったスリットダイを備えた含浸用押出機中で樹脂圧により、炭素繊維ロービングに樹脂を含浸・脱泡する。下流開口部から吐出されたテープ状の炭素繊維とポリプロピレン樹脂からなる複合材料を冷却してかせに巻き取る。さらに、このテープ状複合材料を10mm以上にカットすることや、テープ状複合材料をカットせずに織物状に織って成形用に提供される。または、下流の出口ダイにロービング状炭素繊維を供給して、繊維の送り速度と樹脂の吐出量を調節して、所定の繊維含有率からなるストランド状の炭素繊維の樹脂被覆材を得る。このストランドを冷却してかせに巻き取る。このストランドを10mm以上にカットするか、織物状に織って成形用に提供される方法などが上げられる。
In addition to the above essential components, the molded product of the present invention contains crystal nucleating agents, lubricants, antioxidants, flame retardants, light proofing agents, weathering agents, etc. for the purpose of improving physical properties, improving moldability, and improving durability. it can.
The method for producing the composite material of the present invention is not particularly limited. For example, a polypropylene resin and / or a polypropylene resin copolymer is premixed in a predetermined ratio and supplied to a hopper of a screw type extruder whose temperature is adjusted to be equal to or higher than the melting point of the polypropylene resin. The molten resin is measured at the number of revolutions of the gear pump and supplied upstream of the impregnation extruder whose temperature is adjusted to be equal to or higher than the melting point of the resin. On the other hand, roving-like carbon fibers are expanded and supplied downstream of the impregnation extruder. Carbon fiber roving is impregnated and defoamed with resin pressure in an extruder for impregnation equipped with a slit die having a narrowed opening at the downstream end. The composite material composed of the tape-like carbon fiber and the polypropylene resin discharged from the downstream opening is cooled and wound up. Furthermore, the tape-like composite material is cut into 10 mm or more, or the tape-like composite material is woven into a woven shape without being cut and provided for molding. Alternatively, a roving carbon fiber is supplied to a downstream exit die, and a fiber coating speed and a resin discharge amount are adjusted to obtain a strand-like carbon fiber resin coating material having a predetermined fiber content. The strand is cooled and wound into skeins. A method of cutting the strand into 10 mm or more, or weaving it into a woven shape and providing it for molding can be raised.

本発明の複合材は、赤外線加熱や高周波加熱して、樹脂を加熱溶融して、圧縮成形機にセットされた金型に供給される。金型温度は、前述の理由により好ましくは、135℃以上、特に好ましくは135〜160℃の金型に供給して、賦形冷却後脱型して構造材の部品が成形される。金型温度は、成形中一定とせず、加熱―冷却のサイクルプロセスをとることができる。急速加熱には、電熱加熱に加え、誘導加熱や赤外線加熱などが利用される。また急速冷却には、熱湯やオイルが回路に循環される。
本発明による荷重たわみ温度は160℃を超えることが好ましい。また曲げ強さは、ポリプロピレンの変性度と結晶化度に依存する。酸変性ポリプロピレンを母相とする場合、330MPaを超えることが好ましく、未変性ポリプロピレンの場合110MPaを超えることが好ましい。特に、酸変性ポリプロピレンを使用し、特定の結晶性を高めた成形からえられる曲げ強さである340MPaを超えた成形品が好ましい。
The composite material of the present invention is supplied to a mold set in a compression molding machine by heating and melting the resin by infrared heating or high-frequency heating. The mold temperature is preferably supplied to a mold having a temperature of 135 ° C. or higher, particularly preferably 135 to 160 ° C. for the above-described reason, and after forming cooling, the mold is removed to form a structural material part. The mold temperature is not constant during molding, and a cycle process of heating and cooling can be taken. For rapid heating, induction heating or infrared heating is used in addition to electric heating. For rapid cooling, hot water or oil is circulated in the circuit.
The deflection temperature under load according to the present invention preferably exceeds 160 ° C. Further, the bending strength depends on the degree of modification and crystallinity of polypropylene. When acid-modified polypropylene is used as a parent phase, it is preferably over 330 MPa, and in the case of unmodified polypropylene, it is preferably over 110 MPa. In particular, a molded product that uses acid-modified polypropylene and exceeds 340 MPa, which is a bending strength obtained from molding with improved specific crystallinity, is preferable.

本発明の複合材から得られた成形部品は、自動車のフレーム、バンパーフェースバーサポート材、シャシーシェル、座席フレーム、サスペンジョン支持部、サンルーフフレーム、バンパービーム、2輪車のフレーム、農機具のフレーム、OA機器のフレーム、機械部品など高い強度と剛性の必要な部品に利用される。   Molded parts obtained from the composite material of the present invention include automobile frames, bumper face bar support materials, chassis shells, seat frames, suspension support parts, sunroof frames, bumper beams, two-wheeled vehicle frames, farm equipment frames, OA. Used for parts that require high strength and rigidity, such as equipment frames and machine parts.

以下に実施例を示して本発明を具体的に説明するが、本発明は実施例に限定されるものではない。
(実施例1〜6)
炭素繊維のロービングを所定量になる速度で拡張開繊して押出機のダイヘッドに供給した。一方、種々のポリプロピレン樹脂、変性ポリプロピレン樹脂を、80℃にて1時間乾燥後、シリンダー温度230℃に温度調節された二軸押し出し機(日本製鋼所TEX30α)のホッパーに供給し、可塑化した。炭素繊維の引き抜き速度とポリプロピレン樹脂の供給量を変化して、炭素長繊維の質量分率を変えて種々のサンプルを得た。幅10mm・高さ0.2mmのダイから含浸被覆されたテープ状プリプレグを水槽に浸漬して固化した後、枷に巻き取った。
テープ状プリプレグを35mm長さにカットし、短冊状プリリプレグを得た。コンソリ化プレート厚さ400mm×400mm×2mmに相当する短冊状プリプレグを400mm×400mm×5mmの枠内に面内ランダムになるようにばらまき、予め230℃に温度調節した金型をセットした圧縮成形機を使用して圧縮し、金型を100℃に冷却した後、型開きをして、プリプレグシートを得た。このプリプレグテープをIRヒータにより、230℃に予熱した後、温度100〜150℃に温度調節された400mm×400mm×2mmの金型にセットして、30分間30MPa圧縮保持した。金型を圧縮成形機から取り出した。得られた平板から10mm×100mm×2mmの曲げ試験用テストピース成形品を切削し、40本を得た。
なお、成形品の脱型性を、○:容易に脱型可能、△:真鍮製へらの使用で脱型可能、×:製品を一部破壊しないと脱型できないという3クラス評価分けした。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to the examples.
(Examples 1-6)
The carbon fiber roving was expanded and opened at a predetermined speed and supplied to the die head of the extruder. On the other hand, various polypropylene resins and modified polypropylene resins were dried at 80 ° C. for 1 hour, and then supplied to a hopper of a twin-screw extruder (Nippon Steel Works TEX30α) adjusted to a cylinder temperature of 230 ° C. for plasticization. Various samples were obtained by changing the carbon fiber drawing rate and the amount of polypropylene resin supplied, and changing the mass fraction of carbon long fibers. A tape-shaped prepreg impregnated and coated from a die having a width of 10 mm and a height of 0.2 mm was immersed in a water bath and solidified, and then wound on a basket.
The tape-shaped prepreg was cut into a length of 35 mm to obtain a strip-shaped prepreg. A compression molding machine in which strip-shaped prepregs corresponding to a consolidated plate thickness of 400 mm x 400 mm x 2 mm are randomly distributed within a 400 mm x 400 mm x 5 mm frame and a mold whose temperature is adjusted to 230 ° C in advance is set. After the mold was cooled to 100 ° C., the mold was opened to obtain a prepreg sheet. This prepreg tape was preheated to 230 ° C. with an IR heater, and then set in a 400 mm × 400 mm × 2 mm mold whose temperature was adjusted to 100 to 150 ° C., and compressed and held at 30 MPa for 30 minutes. The mold was removed from the compression molding machine. A test piece molded product for bending test of 10 mm × 100 mm × 2 mm was cut from the obtained flat plate to obtain 40 pieces.
In addition, the demolding property of the molded product was classified into three classes: ○: easy demolding, Δ: demolding using a brass spatula, x: demolding without partial destruction of the product.

(1)曲げ特性
得られた曲げ試験用テストピース各40本を、デシケータ中で23℃にて48時間保管後、ISO178に準拠した3点曲げ試験機(オリエンテック社製テンシロン4L型)を使用して、スパン長80mm、クロスヘッド速度1mm/minによる曲げ強度と曲げ弾性率を測定し、それぞれの平均値を得た。
(2)X線回折
曲げ試験片用テストピースから、10mm×10mm×2mm切り出し、得られた試験片をX線解析装置の試料台にセットした。CuKαのX線源に、40KV,200mAの電荷を掛けたX線解析装置(理学電機製RINT2500)を使用して、2θが10度から40度まで0.1°/分の速度で入射走査して、その回折強度を測定した。回折強度をグラフ表示して、そのプロファイルから結晶形態を推察した。
(4)示差走査熱量(DSC)分析
TA instruments社製Q100型DSCを使用し、試験片から5mg試験片をアルミパンに採取した。これを試験槽にセットし、窒素40ml/分流動しながら、10℃/分にて、200℃まで昇温するために必要なヒートフローをブランクと比較測定した。ヒートフローの多重吸熱ピーク温度を融点として整理した。また120℃と180℃のヒートフロー点を直線で結ぶ直線をベースラインとして、ベースラインとヒートフロー曲線で囲まれる面積から融解熱を算定した。また、150℃と170℃間で最も高い吸熱値を示す吸熱ピーク値と2番目に高い吸熱値を示す吸熱ピーク値とベースライン間のそれぞれの高さを計測し、最も高い吸熱値を示す吸熱ピーク値に対する2番目に高い吸熱値を示す吸熱ピーク値の比率を算定した。
(5)熱重量分析
(4)にてDSC測定済みアルミパンの蓋を開き、試験後の試料を取り出した。熱重量分析装置TA instruments社製Q50を使用し、TGAの炉内にセットした。窒素布雰囲気中で20℃/分にて室温から600℃まで昇温し,600℃にて5分保持して重量変化を測定した。100℃から600℃5分保持の間の重量減少率を測定し、これを樹脂分率と見なし算定した。
(6)荷重たわみ温度
曲げ試験片用に成形したシートから、繊維軸に対して0度方向の曲げ試験片と同様に切削して、10mm×100mm×2mmの試験片4本を得た。HDT試験機(東洋精機社製)を使用して、JIS K7191−1,−2に準拠して、表裏各2本をフラットワイズ状態で1.82MPaの荷重下で2℃/分にて昇温して、支点間中央部のひずみが0.2%に達する温度として測定し、4本の平均温度を求めた。
実施例について、得られたデータを表1に示した。
(1) Bending characteristics 40 pieces of the obtained test pieces for bending test were stored in a desiccator at 23 ° C for 48 hours, and then a three-point bending tester (Tensilon 4L type manufactured by Orientec Co., Ltd.) compliant with ISO178 was used. Then, the bending strength and the bending elastic modulus at a span length of 80 mm and a crosshead speed of 1 mm / min were measured, and average values were obtained.
(2) 10 mm × 10 mm × 2 mm was cut out from the test piece for X-ray diffraction bending test piece, and the obtained test piece was set on the sample stage of the X-ray analyzer. Using an X-ray analyzer (RINT2500, manufactured by Rigaku Corporation) with an electric charge of 40 KV and 200 mA applied to a CuKα X-ray source, 2θ is incident scanned at a rate of 0.1 ° / min from 10 degrees to 40 degrees. The diffraction intensity was measured. The diffraction intensity was displayed in a graph, and the crystal form was inferred from the profile.
(4) Differential scanning calorimetry (DSC) analysis
Using a Q100 DSC manufactured by TA instruments, a 5 mg test piece was collected from the test piece in an aluminum pan. This was set in a test tank, and the heat flow required for heating up to 200 ° C. at 10 ° C./min was measured in comparison with the blank while flowing 40 ml / min of nitrogen. Multiple endothermic peak temperatures of heat flow were arranged as melting points. The heat of fusion was calculated from the area surrounded by the base line and the heat flow curve with the straight line connecting the heat flow points at 120 ° C. and 180 ° C. as the base line. Also, the endothermic peak value showing the highest endothermic value between 150 ° C and 170 ° C, the endothermic peak value showing the second highest endothermic value, and the height between the baselines are measured, and the endothermic value showing the highest endothermic value. The ratio of the endothermic peak value indicating the second highest endothermic value with respect to the peak value was calculated.
(5) Thermogravimetric analysis The lid of the aluminum pan after DSC measurement was opened in (4), and the sample after the test was taken out. A thermogravimetric analyzer Q50 manufactured by TA instruments was used and set in a TGA furnace. The temperature was raised from room temperature to 600 ° C. at 20 ° C./min in a nitrogen cloth atmosphere and held at 600 ° C. for 5 minutes to measure the change in weight. The weight reduction rate was measured between 100 ° C. and 600 ° C. for 5 minutes, and this was regarded as the resin fraction and calculated.
(6) Deflection temperature under load From the sheet formed for the bending test piece, cutting was performed in the same manner as the bending test piece in the direction of 0 degree with respect to the fiber axis, and four test pieces of 10 mm × 100 mm × 2 mm were obtained. Using an HDT tester (manufactured by Toyo Seiki Co., Ltd.), in accordance with JIS K7191-1 and -2, the two sides of the front and back are heated at 2 ° C / min under a load of 1.82 MPa in a flatwise state. Then, the temperature was measured as the temperature at which the strain at the center between the fulcrums reached 0.2%, and the average temperature of the four was obtained.
The data obtained for the examples are shown in Table 1.

(比較例1〜6)
ポリプロピレン樹脂の種類や炭素繊維の質量分率を変更した以外は、実施例と全く同様に、コンパウンドペレットやそれを用いたプリプレグを作製した後、テストピースを成形した。得られた試験片について,実施例と全く同様に0度曲げ強度と90度曲げ強度、荷重たわみ温度、プリプレグについて、X線回折強度比、DSC分析、TGA分析を測定した。得られた試験データを表2に示した。
(Comparative Examples 1-6)
Except that the type of polypropylene resin and the mass fraction of carbon fiber were changed, compound pellets and prepregs using the same were produced in the same manner as in the Examples, and then test pieces were molded. About the obtained test piece, the X-ray diffraction intensity ratio, DSC analysis, and TGA analysis were measured about 0 degree bending strength and 90 degree bending strength, the deflection temperature under load, and the prepreg just like the Example. The test data obtained is shown in Table 2.

実験に使用した原料と記号
PP−1:無水マレイン酸変性ポリプロピレン(東洋紡績製試作品、ホモポリプロピレンに、無水マレイン酸と半減期1分が178℃有機過酸化物を配合し、200℃で1分溶融加熱して得た。メルトフローレート85g/10min, 無水マレイン酸分率0.3%)
PP−2:ポリプロピレン(プライムポリマー社製、ホモポリプロピレン、J139,メルトフローレート 60g/10min, 無水マレイン酸率0%)
炭素繊維:帝人社製 東邦テナックス IMS40(単繊維径6.4μm、6000フィラメント)
Raw materials used in the experiment and symbol PP-1: Maleic anhydride-modified polypropylene (Toyobo's prototype, homopolypropylene, blended with maleic anhydride and organic peroxide having a half-life of 1 minute at 178 ° C., 1 at 200 ° C. (Melting and heating, melt flow rate 85g / 10min, maleic anhydride fraction 0.3%)
PP-2: Polypropylene (manufactured by Prime Polymer, Homopolypropylene, J139, melt flow rate 60 g / 10 min, maleic anhydride rate 0%)
Carbon fiber: Toho Tenax IMS40 (single fiber diameter 6.4 μm, 6000 filaments) manufactured by Teijin Limited

本発明の効果により、荷重たわみ温度は5℃上昇している。曲げ強さと曲げ弾性率は、母相をなすポリプロピレンの物性にも大変依存する。同一のポリプロピレンを使用した、実施例1と比較例1、実施例2と比較例2をそれぞれ比較すると、弾性率は殆ど同じであるが、成形条件により特殊な結晶融解挙動を有する実施例の曲げ強さは、比較例より高い曲げ強さを有している。 Due to the effect of the present invention, the deflection temperature under load is increased by 5 ° C. Flexural strength and flexural modulus are also highly dependent on the physical properties of the polypropylene that forms the matrix. When Example 1 and Comparative Example 1, Example 2 and Comparative Example 2 were compared using the same polypropylene, the elastic modulus was almost the same, but the bending of the example having a special crystal melting behavior depending on molding conditions. The strength is higher than that of the comparative example.

本発明により、曲げ強度に優れたスタンピング成形品を得ることが可能となり、比重が比較的小さく、プリプレグ製造法や成形法も非常に容易であることからも、構造部材やハウジングの樹脂化が可能となり、軽量化や省エネルギーの面から産業界に大きく寄与することが期待される。   The present invention makes it possible to obtain stamped molded products with excellent bending strength, relatively low specific gravity, and extremely easy prepreg manufacturing and molding methods, allowing structural members and housings to be made of resin. Therefore, it is expected to make a significant contribution to the industry in terms of weight reduction and energy saving.

Claims (4)

炭素長繊維を40〜75質量%含有し、示差走査熱量計のヒートフロー曲線が150℃〜170℃の間に2つ以上の吸熱ピークもつポリプロピレンを25〜60質量%含有する炭素長繊維強化ポリプロピレンを成形してなることを特徴とする炭素長繊維強化ポリプロピレン成形品。   Carbon long fiber reinforced polypropylene containing 40 to 75% by mass of carbon long fiber and 25 to 60% by mass of polypropylene having two or more endothermic peaks between 150 ° C. and 170 ° C. in the heat flow curve of the differential scanning calorimeter A carbon long fiber reinforced polypropylene molded product characterized by being molded. 前記ポリプロピレンが、150℃〜170℃の間のヒートフロー曲線の吸熱ピークの中で、最も高い吸熱値を示す吸熱ピークの吸熱値に対して2番目に高い吸熱値を示す吸熱ピークの吸熱値がその60%以上であることを特徴とする請求項1に記載の炭素長繊維強化ポリプロピレン成形品。   In the endothermic peak of the heat flow curve between 150 ° C. and 170 ° C., the endothermic value of the endothermic peak showing the second highest endothermic value with respect to the endothermic value of the endothermic peak showing the highest endothermic value is obtained. The carbon long fiber reinforced polypropylene molded product according to claim 1, which is 60% or more. 樹脂成分1g当たりの融解熱が、97J以上であることを特徴とする請求項1に記載の炭素長繊維強化ポリプロピレン成形品。 2. The carbon long fiber reinforced polypropylene molded article according to claim 1, wherein the heat of fusion per 1 g of the resin component is 97 J or more. 成形部分の表面温度が135℃以上である金型を使用して圧縮成形されたことを特徴とする請求項1〜3のいずれかに記載の炭素長繊維強化ポリプロピレン成形品。 The carbon long fiber reinforced polypropylene molded article according to any one of claims 1 to 3, wherein the molded part is compression molded using a mold having a surface temperature of 135 ° C or higher.
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