[0019] 以下，詳細說明本發明。 本發明之FRP成形用材料之基質樹脂係以苯氧基樹脂(A)、環氧樹脂(B)及交聯劑(C)作為必要成分而構成之無溶劑系之常溫固態之苯氧基樹脂組成物，(A)、(B)、(C)之各成分以維持反應性之狀態直接附著於強化纖維基材。 [0020] 本發明之FRP成形用材料中，作為基質樹脂組成物之必須成分使用之苯氧基樹脂(A)較好為常溫下為固態且於220℃之之熔融黏度為1×104
Pa．s以下者。熔融黏度較好為1×102
~6×103
Pa．s，更好為2×102
~3×103
Pa．s。熔融黏度超過1×104
Pa．s時，由於成形加工時之樹脂流動性變差，故樹脂未充分行進至纖維基材內而成為孔洞之原因，會使成形物之機械物性降低。 [0021] 苯氧基樹脂(A)係使2元酚化合物與表鹵醇之縮合反應或2元酚化合物與2官能環氧樹脂之聚加成反應所得之熱塑性樹脂，可於溶劑中或無溶劑下藉以往習知之方法獲得。平均分子量以質量平均分子量(Mw)計，通常為10,000~200,000，但較好為20,000~100,000，更好為30,000 ~80,000。Mw若過低，則成形體強度差，若過高則易成為作業性或加工性差者。又，Mw係表示以凝膠滲透層析法測定，使用標準聚苯乙烯校正線換算之值。 [0022] 又，苯氧基樹脂(A)之羥基當量(g/eq)通常為50~1000，較好為100~750，特佳為200~500。羥基當量過低時，由於羥基增加而使吸水率提高，故有機械物性降低之顧慮而欠佳，羥基當量過高時，交聯密度不足而降低耐熱性。 [0023] 苯氧基樹脂(A)之玻璃轉移溫度(Tg)宜為65℃~150℃以下者，較好為70℃~100℃，更好為80℃~100℃。玻璃轉移溫度低於65℃時，成形性雖良好，但粉體之儲存安定性或FRP成形材料之觸黏性產生問題。高於150℃時熔融黏度亦變高而使成形性或對纖維之填充性差，結果必須於更高溫壓製成形。又，苯氧基樹脂之玻璃轉移溫度係使用示差掃描熱量測定裝置(DSC)，以10℃/分鐘之升溫條件，於20~280℃之範圍測定，由第二次掃描之峰值計算之數值。 [0024] 作為苯氧基樹脂(A)只要滿足上述物性者則未特別限制，但可舉例為雙酚A型苯氧基樹脂(例如新日鐵住金化學公司製PHENOTOTO YP-50、PHENOTOTO YP-50S、PHENOTOTO YP-55U)、雙酚F型苯氧基樹脂(例如新日鐵住金化學公司製PHENOTOTO FX-316)、或雙酚A與雙酚F之共聚合型苯氧基樹脂(例如新日鐵住金化學公司製YP-70)、前述以外之特殊苯氧基樹脂(例如新日鐵住金化學公司製YPB-43C、FX293)等，該等可單獨使用或混合2種以上使用。 [0025] 於本發明之FRP成形用材料中使用之基質樹脂組成物中，可與苯氧基樹脂(A)一起摻合環氧樹脂(B)。藉由並存環氧樹脂(B)，除了降低基質樹脂組成物之熔融黏度而提高對強化纖維基材之含浸性以外，亦可提高硬化成形物之強度物性。 該情況下，基質樹脂組成物之熔融黏度基本上取決於苯氧基樹脂之熔融黏度，但受到環氧樹脂之摻合量或交聯劑種類等之影響。例如環氧樹脂之摻合量較多時，基質樹脂組成物之熔融年度降低，若交聯劑不適當，則由於融融黏度因快速反應而無法降低，故有必要進行適當調整。 環氧樹脂(B)較好為2官能性以上之環氧樹脂，舉例雙酚A型環氧樹脂(例如新日鐵住金化學股份有限公司製EPOTOTO YD-011、EPOTOTO YD-7011、EPOTOTO YD-900)、雙酚F型環氧樹脂(例如新日鐵住金化學股份有限公司製EPOTOTO YDF-2001)、二苯基醚型環氧樹脂(例如新日鐵住金化學股份有限公司製YSLV-80DE)、四甲基雙酚F型環氧樹脂(例如新日鐵住金化學股份有限公司製YSLV-80XY)、雙酚硫醚型環氧樹脂(例如新日鐵住金化學股份有限公司製YSLV-120TE)、氫醌型環氧樹脂(例如新日鐵住金化學股份有限公司製EPOTOTO YDC-1312)、酚酚醛清漆型環氧樹脂(例如新日鐵住金化學股份有限公司製EPOTOTO YDPN-638)、鄰甲酚酚醛清漆型環氧樹脂(例如新日鐵住金化學股份有限公司製EPOTOTO YDCN-701、EPOTOTO YDCN-702、EPOTOTO YDCN-703、EPOTOTO YDCN-704)、芳烷基萘二酚酚醛清漆型環氧樹脂(例如新日鐵住金化學股份有限公司製ESN-355)、三苯基甲烷型環氧樹脂(例如日本化藥股份有限公司製EPPN-502H)等，但不限定於該等，且亦可將該等混合2種以上使用。 [0026] 又，為了使基質樹脂組成物作為粉體予以保存，關於環氧樹脂(B)亦更好於室溫為固體，宜為熔點係75℃~145℃，且於160℃下之熔融黏度為1.0Pa．s以下之結晶性環氧樹脂。超過1.0Pa．s時，基質樹脂組成物對強化纖維基材之填充性差，所得成形體之均質性差故而欠佳。 又，結晶性環氧樹脂，由於其熔融黏度遠低於固態環氧樹脂，故藉由摻合結晶性環氧樹脂，可提高基質樹脂之含浸性。因此可使用高熔融黏度之苯氧基樹脂。 [0027] 本發明所用之交聯劑(C)可使用具有2個以上可與苯氧基樹脂所具有之2級羥基及環氧樹脂之環氧基反應之官能基者，且為上述一般式(1)~(3)表示之酸酐。由於一個酸酐基因水解而產生2個羧基，故可理解為具有2個上述官能基。 又，作為交聯劑之酸酐係藉由與苯氧基樹脂之2級羥基形成酯鍵而使苯氧基樹脂三次元交聯。因此，與如熱硬化性樹脂之硬化般之強固交聯不同，而可藉由水解反應等解開交聯，故於回收性不產生阻礙。 [0028] 酸酐若在常溫為固體且昇華性低者，則可作為交聯劑(C)使用，但本發明中，基於對成形物賦予耐熱性或增加交聯密度之觀點，為芳香族四羧酸二酐，且係一般式(1)~(3)所示之至少1種的芳香族四羧酸二酐。式中，X表示O、-CH2
-、-C(CH3
)-、-(Ph)m
-、 -Ph-CH2
-Ph-或-Ph-C(CH3
)2
-Ph-，Ph為伸苯基，m為1至4的整數。 式中，Y表示-(CH2
)m
-、-(Ph)m
-、-Ph-CH2
-Ph-或 -Ph-C(CH3
)2
-Ph-，Ph為伸苯基，m為1至4的整數。 又，X、Y之說明中，若以構造式表示-(Ph)m
-、 -Ph-CH2
-Ph-或-Ph-C(CH3
)2
-Ph-則為如以下者，但鍵結鍵不限於構造式所示之對位，而可為間位亦可為鄰位，交聯劑若能溶解於熔融的苯氧基樹脂與環氧樹脂，而可使基質樹脂組成物成為透明，則可使用。[0029] 該等一般式(1)~(3)所示之芳香族四羧酸二酐由於大多是交聯劑本身藉由熱而熔融之前，不易與基質樹脂組成物之主成分的苯氧基樹脂或環氧樹脂相溶，故藉由使交聯反應從低溫開始就不會引起熔融黏度增加。因此，成形加工時由於基質樹脂組成物熔融成為充分低黏度後才開始交聯反應，故基質樹脂對於強化纖維基材之含浸性良好以外，由於交聯反應不會過快亦不會過於不足地進行，故不會以未反應狀態作為異物殘留於基質樹脂中，而不會產生以殘留之交聯劑(C)為起點之成形物之機械強度或加熱中之機械強度降低之問題。 又，關於交聯劑(C)與苯氧基樹脂(A)及環氧樹脂(B)之相溶性，可藉由使該等之混合物的基質樹脂組成物於200℃熔解並混練，目視觀察冷卻後之反應應化物而評價透明性予以進行。 [0030] 作為此等芳香族四羧酸二酐，舉例為4,4’-氧基二鄰苯二甲酸酐或4,5’-氧基二鄰苯二甲酸酐、5,5’-亞甲基雙(異苯并呋喃-1,3-二酮)、5,5’-異亞丙基雙(異苯并呋喃-1,3-二酮)、乙二醇雙苯偏三酸酐、雙(1,3-二氧代異苯并呋喃-5-羧酸)四亞甲基、4,5’-[1,4-伸苯基雙(氧基)]雙(異苯并呋喃-1,3-二酮)、4,4’-(間-伸苯基雙氧基)雙(異苯并呋喃-1,3-二酮)、5,5’-[1,3-伸苯基雙(氧基)]雙(異苯并呋喃-1,3-二酮)、3,3’-(對-伸苯基二氧基)二鄰苯二甲酸酐、5,5’-[1,2-伸苯基雙(氧基)]雙(異苯并呋喃-1,3-二酮)、4,4’-[2,1-伸苯基雙(氧基)]雙(異苯并呋喃-1,3-二酮)、4,4’-(對-伸苯基二氧基)二鄰苯二甲酸酐、5,5’-[聯苯-4,4’-二基雙(氧基)]雙(異苯并呋喃-1,3-二酮)、5,5’-[聯苯-2,2’-二基雙(氧基)]雙(異苯并呋喃-1,3-二酮)、雙酚A、二鄰苯二甲酸酐、2,2’-二(4-苯偏三醯氧基)聯苯二酐、2,2’-雙(4-羥基苯基)丙烷二苯甲酸酯-3,3’,4,4’-四羧酸二酐、雙(1,3-二氧代異苯并呋喃-5-羧酸)異亞丙基雙(4,1-伸苯基)、3,3’-二苯基-4,4’-聯酚-雙(苯偏三酸酐)等，其中最好以選自4,4’-氧基二鄰苯二甲酸酐、乙二醇雙苯偏三酸酐、4,4’-(1-甲基亞乙基)二鄰苯二甲酸酐之至少一種芳香族四羧酸作為交聯劑(C)。 [0031] 苯氧基樹脂(A)、環氧樹脂(B)及交聯劑(C)之反應係藉由使苯氧基樹脂(A)中之2級羥基與交聯劑(C)之酸酐基之酯化反應，進而藉由該酯化反應生成之羧基與環氧樹脂(B)之環氧基反應而交聯、硬化。藉由苯氧基樹脂(A)與交聯劑(C)之反應雖可獲得苯氧基樹脂交聯體，但藉由共存環氧樹脂(B)，除了可減低基質樹脂組成物之熔融黏度提高對強化纖維基材之含浸性以外，由於可獲得促進交聯反應、提高交聯密度、提高機械強度等優異之FRP成形體故而為較佳之FRP成形用材料。又，本發明中，雖共存環氧樹脂(B)，但認為以熱塑性樹脂的苯氧基樹脂(A)作為主成分，且其2級羥基與交聯劑(C)之酸酐基之酯化反應較優先。亦即，作為交聯劑(C)使用之酸酐與環氧樹脂(B)之反應耗費時間，故首先引起與苯氧基樹脂(A)之2級羥基之反應，若交聯劑(C)的酸酐失活，則與環氧樹脂(B)之反應性大為降低。因此，本發明之FRP成形用材料與以熱硬化性樹脂的環氧樹脂為主成分之通常之FRP成形用材料不同，為即使長期室溫保管後，亦可維持成形性或FRP成形物之物性，儲存安定性優異。 [0032] 又，本發明之苯氧基樹脂組成物中，亦可摻合硬化促進劑(D)。硬化促進劑(D)若於常溫為固體且無昇華性者則並未特別限定，舉例為例如三伸乙基二胺等之3級胺，2-甲基咪唑、2-苯基咪唑、2-苯基-4-甲基咪唑等之咪唑類，三苯膦等之有機膦類、四苯基鏻四苯基硼酸鹽等之四苯基硼鹽等。該等促進劑(D)可單獨使用亦可併用2種以上。且基於本發明之製造製程之觀點，較好使用觸媒活性溫度為130℃以上之常溫為固體之咪唑類潛在性觸媒的硬化促進劑。 [0033] 再者，本發明之FRP成形用材料中，於不損及對強化纖維基材之附著性或成形物之FRP成形體之物性之範圍內，亦可摻合其他熱塑性樹脂粉末例如聚氯乙烯樹脂、聚偏氯乙烯樹脂、天然橡膠、合成橡膠等之粉末，或各種無機填料、體質顏料、著色劑、抗氧化劑、紫外線防止劑等之其他添加物。 [0034] 本發明之FRP成形用材料之基質樹脂組成物係藉由將必須成分的苯氧基樹脂(A)、環氧樹脂(B)及交聯劑(C)、進而根據需要之硬化促進劑(D)或耐濕顏料、著色劑、其他添加劑粉碎為特定大小後，以特定摻合比例混合，並使該基質樹脂微組成物以粉體狀態附著於強化纖維基材而獲得。 [0035] 本發明之基質組成物係以相對於苯氧基樹脂(A)100重量份而言成為5~85重量份之方式摻合環氧樹脂(B)。較好為9~83重量份，更好為10~70重量份。環氧樹脂之摻合量超過85重量份時，由於環氧樹脂硬化需要時間，故除了難以於短時間獲得脫模所需之強度以外，FRP之回收性亦降低。又，環氧樹脂(B)之摻合量未達5重量份時，無法獲得摻合環氧樹脂所致之效果，基質樹脂組成物之硬化物難以展現160℃以上之Tg。 [0036] 基質樹脂組成物於常溫為固態，其熔融黏度於160~220℃之溫度區域之任一溫度中為3,000Pa．s以下。160~220℃係通常進行熱加壓成形之溫度區域。較好為2,900Pa．s以下，更好為2,800Pa．s。熔融黏度若超過3,000Pa．s，則藉由熱加壓而成形時基質樹脂組成物對強化纖維基材之含浸變不充分，產生內部孔隙等之缺陷，使FRP之機械物性降低。 又，熔融黏度於基質樹脂組成物中之苯氧基樹脂(A)及環氧樹脂(B)與交聯劑(C)反應時將急遽上升。因此，若於苯氧基樹脂(A)與環氧樹脂(B)未充分熔融前即與交聯劑(C)開始反應，則熔融黏度不會成為3,000Pa．s以下，引起基質樹脂對強化纖維基材之含浸不良，於成形體中產生孔隙。因此，交聯劑(C)之熔點期望為150℃以上，較好為成形溫度(160~220℃)之範圍。 [0037] 交聯劑(C)之摻合量，通常為相對於苯氧基樹脂(A)之2級羥基1莫耳，酸酐基0.6~1.3莫耳之範圍的量，較好為0.9~1.3莫耳之範圍的量，更好為0.9~1.1莫耳之範圍。酸酐基之量過少時，由於相對於苯氧基樹脂(A)之2級羥基，反應性酸酐基不足，故交聯密度低剛性差，過多時相對於苯氧基樹脂(A)之2級羥基，酸酐基過量而未反應之酸酐對硬化特性或交聯密度造成不良影響。又，認為藉由交聯劑之酸酐基(COOH)不僅直接使苯氧基樹脂交聯，亦有透過環氧樹脂使苯氧基樹脂交聯而並存2種形態，推定係交聯劑之酸酐基，及酸酐基開環而得之羧基被苯氧基樹脂之2級羥基與環氧樹脂之環氧基消耗，於硬化物中幾乎無殘存之羧基。 [0038] 除了必須成分(A)~(C)以外，亦使用硬化促進劑(D)時，(D)之摻合量相對於苯氧基樹脂(A)、環氧樹脂(B)及交聯劑(C)之合計量100重量份，設為0.1~5重量份。關於其他添加劑，係適當調整為不損及基質樹脂組成物粉末對基材之附著或成形物之特性之範圍而添加。 [0039] 再者，本發明之FRP成形用材料中，期望添加難燃劑。難燃劑若常溫為固體且無昇華性者即無特別限制，但基於環境或健康等之影響，較好使用非鹵素系難燃劑，舉例為例如如氫氧化鈣之無機系難燃劑、或如磷酸銨類或磷酸酯化合物之有機系及無機系之磷系難燃劑，三嗪化合物等之含氮系難燃劑、溴化苯氧基樹脂等之含溴系難燃劑等。其中溴化苯氧基樹脂或含磷苯氧基樹脂由於可作為難燃劑兼基質樹脂使用故可較好地使用。關於難燃劑之摻合量，雖根據難燃劑種類或期望難燃性程度而適當選擇，但較好對於基質樹脂組成物100重量份大概為0.01~10重量份之範圍內，於無損基質樹脂組成物之附著性或FRP成形物之物性之程度內摻合。 [0040] 本發明之FRP成形用材料之製造方法中，構成基質樹脂組成物之各成分係作成為微粉末附著於強化纖維基材。因此，各成分係經粉碎成為微粉末。該粉碎較好使用低溫乾燥粉碎機(離心乾燥研磨機)等之粉碎混合機，但不限定於該等。又，粉碎時亦可將各成分粉碎後混合，亦可預先摻合各成分後粉碎，但較好為前者。該情況下，只要設定粉碎條件以使各微粉末成為後述之平均粒徑即可。作為如此獲得之粉末，平均粒子徑為10~100μm，較好為40~80μm，更好為40~50μm。平均粒徑超過100μm時，於靜電場中之粉體塗裝中附著於強化纖維基材時，樹脂衝撞纖維時之能量變大，會降低對強化纖維基材之附著率。且若為未達10μm，則粒子因伴隨氣流而飛散而使附著效率降低以外，於大氣中浮游之微粉樹脂亦有引起作業環境惡化之可能性。且此時，苯氧基樹脂(A)及環氧樹脂(B)粉末之平均粒徑較好為交聯劑(C)之平均粒徑之1~1.5倍。藉由使交聯劑(C)粉末之粒徑比苯氧基樹脂(A)及環氧樹脂(B)之各粉末更微細，可使交聯劑(C)附著至強化纖維基材內部，並且交聯劑(C)不會滿遍於(A)、(B)成分之粒子周圍而存在，而可確實進行交聯反應。 [0041] 藉由粉體塗裝法將基質樹脂組成物之粉末附著於強化纖維基材而獲得本發明之FRP成形用材料。粉體塗裝法有利用流動床之流動塗裝法與利用靜電場之靜電塗裝法，本發明中雖可利用任一方法，但基於對強化纖維基材之附著均一性，較好使用利用靜電場之靜電塗裝法。 [0042] 基質樹脂組成物對強化纖維基材之附著量係以樹脂比例(RC)成為20~50wt%之方式塗佈，但較好為25%~40%，更好為25~30%。樹脂附著率超過50%時，FRP之拉伸．彎曲彈性率等機械物性會降低，低於10%時，由於樹脂附著量極端減少故基材樹脂對基材內部之含浸不充分，使熱物性、機械物性均變低。 [0043] 經粉體塗裝之基質樹脂組成物之粉體藉由加熱熔融而固定於強化纖維基材，但亦可使用塗佈粉體後加熱融合之冷塗裝，與預先對經加熱之強化纖維進行粉體塗裝並融合之熱塗裝之任一種。藉由該加熱熔融，使強化纖維基材表面之基質樹脂熔融而提高對基材之密著性，並防止經塗裝之樹脂粉末脫落。惟，所得FRP材料中基質樹脂集中於強化纖維基材表面，無法如加熱加壓成形後之成形體般行進至強化纖維基材內部。又，進行粉體塗裝後之加熱時間只要FRP成形用材料之基質樹脂組成物可保持流動性及反應性之範圍，則未特別限制，但通常宜為1~2分鐘。亦即，藉由遠比成形時短之時間進行熱處理，不使交聯劑與樹脂反應而藉由熱融合將苯氧基樹脂或環氧樹脂固定於強化纖維基材，防止掉粉。熔融溫度為150~240℃，較好為160~220℃，更好為180~200℃。熔融溫度超過上限時有進行硬化反應之可能性，且低於下限時，熱融合變不充分，於FRP成形用材料之處理時發生基質樹脂掉粉、脫落等。 [0044] 強化纖維基材可使用碳纖維、玻璃纖維、聚芳醯胺纖維、硼纖維、氧化鋁纖維、礦物纖維、碳化矽纖維等，但利用靜電塗裝時由於必須具備導電性，故較好為碳纖維。又強化纖維基材之形態並未特別限制，例如可使用單方向材、平織或綾織等之布、三次元布、切短原絲薄氈(chopped strand mats)、由數千根以上纖絲所成之藤、或不織布等。該等強化纖維基材可使用1種，亦可併用2種以上。 [0045] 如此製作之本發明之FRP成形用材料可為單獨或藉由積層、加熱且加壓而可簡便製造FRP成形物。又，積層時亦可於層間或最外層積層鋁或不鏽鋼等金屬箔等。本發明之FRP成形用材料可藉由熱加壓之加壓成形而同時進行賦形與基質樹脂之交聯與硬化。 使用FRP成形用材料之成形，只要為加熱加壓成形，則可配合成為目的之FRP成形物之大小或形狀，適當選擇使用高壓釜成型或金屬模具之熱加壓成形等之各種成形法而實施。成形溫度為例如150~240℃，較好為160℃~220℃，又更好為180℃~200℃。又，成形溫度超過上述範圍之上限溫度時，由於會施加過量熱而有引起樹脂分解之可能性，且低於下限溫度時由於基質樹脂組成物之熔融黏度提高，故對纖維之含浸性變差。又，關於成形時間，通常為30~60分鐘，但即使為10分鐘左右之短時間，亦可藉由利用作為主成分之苯氧基樹脂(A)之2級羥基之與交聯劑(C)之反應，獲得進行脫模之強度。惟，為使環氧樹脂(B)之硬化反應完成，較好於例如200~250℃後固化30~60分鐘左右。 [0046] 所製造之FRP成形用材料，藉由使基質樹脂組成物利用苯氧基樹脂之2級羥基之交聯反應而使耐熱性比成形前大為上升，獲得Tg為160℃以上之成形物。基質樹脂組成物之軟化點由於在自Tg約-25℃以內，故例如使用金屬模具之熱加壓成形中，成形物自金屬模具之脫模溫度若為基質樹脂組成物之硬化物之自Tg -30℃以下之範圍即可能，較好為硬化物之自Tg -35℃以下，更好自Tg -40℃以下。又，脫模溫度超過上述範圍之上限溫度時，無法保有賦形，且脫模溫度過低時冷卻所需時間變長，故工站時間(tact time)變長，生產性降低。 又，所謂軟化點表示基質樹脂硬化物之藉由DMA所測定之儲存彈性率(E’)產生衰減之拐彎點之溫度。 [0047] 本發明之纖維強化塑膠成形用材料之硬化物係使FRP成形用材料加熱硬化而得者，係上述交聯發達者。該硬化物包含上述纖維強化塑膠成形用材料中之基質樹脂之硬化物與強化纖維基材，該等經強固結合而賦予特定強度等之特性。而且，該基質樹脂組成物之交聯硬化物之玻璃轉移溫度宜為160℃以上。 [0048] 本發明之纖維強化塑膠成形物之製造方法係使上述纖維強化塑膠成形用材料加熱、加壓而硬化、成形者。 [實施例] [0049] 以下顯示實施例，進一步具體說明本發明，但本發明不限定於該等實施例之記載者。 [0050] 實施例及比較例中使用之材料如以下。 [0051] 苯氧基樹脂(A) (A-1)PHENTOTO YP-50S(新日鐵住金化學股份有限公司製雙酚A型，Mw=40,000，羥基當量=284)，200℃下之熔融黏度=3,000Pa．s，玻璃轉移溫度(Tg)=83℃ 環氧樹脂(B) (B-1)：YSLV-80XY(新日鐵住金化學股份有限公司製四甲基雙酚F型，環氧當量=192，熔點：72℃) 交聯劑(C) (C-1)：乙二醇雙偏苯三酸酐 (酸酐當量：207，熔點：160℃，TEMG) (C-2)：4,4’-氧基二鄰苯二甲酸酐 (酸酐當量：153，熔點：225℃，OPDA) (C-3)：雙酚A，二鄰苯二甲酸酐(酸酐當量：260，熔點：184℃，SABIC公司製BisDA) (C-4)：4,4’-雙鄰苯二甲酸酐 (酸酐當量：147，熔點：229℃，BPDA) (C-5)：3,3’,4,4’-二苯甲酮四羧酸二酐 (酸酐當量：161，熔點：218℃，BTDA) (C-6)：3,3’,4,4’-二苯基碸四羧酸二酐 (酸酐當量：179，熔點：≧287℃，DSDA) [0052] 各種物性之試驗及測定方法如下。 [0053] 熔融黏度 基質樹脂組成物等之熔融黏度係使用流變計(Anton Paar公司製)，以平行板夾住樣品尺寸4.3 cm3
，邊以50℃/分鐘升溫，邊以頻率：1Hz、負荷變形：5%之條件，測定160℃之熔融黏度。 [0054] 平均粒徑 基質樹脂組成物粉末等之平均粒徑係藉由雷射繞射．散射式粒徑分佈測定裝置(MICROTRACK MT3300EX，日機裝公司製)，以體積基準進行平均粒徑(D50)測定。 [0055] 樹脂(A)、(B)與交聯劑(C)之相溶性(透明性) 於苯氧基樹脂(A)、環氧樹脂(B)中摻合交聯劑(C)之基質樹脂組成物於200℃熔解並混練，以目視觀察冷卻後之反應應化物並評價透明性而進行。 [0056] 預成形薄片之觸黏性 以手指接觸所得FRP成形用材料表面，無觸黏性者設為合格，於表1中記為○。 [0057] 樹脂比例(RC：%) 使用下述式，自基質樹脂組成物附著前之碳纖維布之重量(W1)與樹脂組成物附著後之FRP成形用材料之重量(W2)而算出。 樹脂比例(RC：%)=(W2-W1)/W2×100 W1：基質樹脂組成物附著前之強化纖維重量 W2：基質樹脂組成物附著後之FRP成形用材料之重量 [0058] 玻璃轉移溫度(Tg)、樹脂軟化溫度 將厚2mm、寬10mm、長10mm之試驗片，使用動態黏彈性測定裝置(Perkin Elmer公司製，DMA 7e)，以5℃/分鐘之升溫條件，於25~250℃之範圍予以測定，將所得之tanδ之極大波峰設為玻璃轉移點。 又樹脂軟化溫度係設為成形物硬化物之同樣試驗片藉由DMA所測定之儲存彈性率(E’)產生衰減之拐彎點之溫度。表示成形硬化後之可脫模溫度。 [0059] 機械物性 FRP成形用材料於鐵氟龍(註冊商標)薄片上重疊13片，以加熱至200℃之加壓機，以5MPa加壓10分鐘，製作FRP層合板後，以烘箱進行1小時後固化，基於JIS K 7074:1988 纖維強化塑膠之彎曲試驗方法，測定所得FRP層合板之機械物性(彎曲彈性率、彎曲強度)。 [0060] 樹脂含浸性 FRP成形用材料於鐵氟龍薄片上重疊13片，以加熱至200℃之加壓機以5MPa加壓5分鐘而製作層合板後，以烘箱進行1小時後固化，使用鑽石切割機切出數片10mm見方之細片。切出之細片以#1000以上之耐水研磨紙研磨切斷面後，藉由光學顯微鏡進行觀察確認有無孔洞。 [0061] FRP成形用材料之室溫保存安定性 於常溫之室內保管3個月之FRP成形用材料於鐵氟龍薄片上重疊13片，以加熱至200℃之加壓機以5MPa加壓5分鐘而製作層合板，以烘箱進行1小時後固化，進行熱物性或機械物性之評價。與3個月前製作之層合板進行比較，物性誤差若為±10%範圍內則為合格，於表1中記為○。 [0062] CFRP之長期耐熱性試驗 以與機械物性測定用之試驗片同樣作成之試驗片於100℃之溫度環境下保持500小時後，基於JIS K 7074:1988 纖維強化塑膠之彎曲試驗方法，進行機械強度測試。 [0063] 實施例1 將作為苯氧基樹脂(A)之(A-1)、作為環氧樹脂(B)之(B-1)、作為交聯劑(C)之(C-1)分別粉碎、分級之平均粒徑D50為80μm(A、B、C之平均粒徑大致相同)之粉體者，以表1所示之比例(重量份)乾摻合，於靜電場中，以電荷70kV、吹附空氣壓0.32MPa之條件於由碳纖維(TOHO TENAX公司製，STANDARD Modulus type HST 403K)所成之經開纖處理之平織強化纖維基材上進行粉體塗裝。隨後，於烘箱中以170℃、1分鐘加熱熔融使樹脂熱融合，獲得FRP成形用材料。所得FRP成形用材料之樹脂比例(RC)為27%。 針對如此所得之FRP成形用材料及FRP硬化物測定各種物性。該等結果示於表1。 [0064] 實施例2、3及比較例1~3 作為交聯劑(C)除了代替(C-1)而使用(C-2)、(C-3)、(C-4)、(C-5)、(C-6)以外，與實施例1同樣，獲得FRP成形用材料，進而獲得FRP層合板，評價各種物性。其結果亦示於表1。 又，關於比較例3之彎曲彈性率與彎曲強度、長期耐熱性，由於基質樹脂脆，故無法測定。 [0065][0066] 由表1所得之結果可知使用C-1、C-2、C-3作為交聯劑(C)之基質樹脂組成物之微粉末附著於強化纖維基材之FRP成形用材料所得之CFRP顯示Tg160℃以上之優異耐熱性，並且由於基質樹脂組成物之熔融黏度低，故對強化纖維基材之含浸性良好，顯示高的機械強度。再者，由於交聯劑對於苯氧基樹脂及環氧樹脂之相溶性良好，故反應性良好，由於未作為固形物殘留，故即使長期暴露於100℃之加熱條件，機械強度之降低亦小。如此本實施例之FRP成形用材料可獲得具備高耐熱性與常溫及加熱之機械物性之FRP成形物，故作為FRP成形用材料非常優異。 [產業上之利用領域] [0067] 本發明之纖維強化塑膠成形用材料作為纖維強化塑膠(FRP)材料，而可於汽車或飛機機器等之運輸機器之車體或機體、筆記型個人電腦或平板電腦之電子機器類之框體及至產業用機器人等之手臂、建築構造物之補強材料或釣竿或公路自行車之運動休閒娛樂領域等之廣泛領域中被利用。[0019] Hereinafter, the present invention will be described in detail. The matrix resin of the FRP molding material of the present invention is a solventless system of a normal temperature solid phenoxy resin comprising a phenoxy resin (A), an epoxy resin (B) and a crosslinking agent (C) as essential components. Each of the components (A), (B), and (C) is directly adhered to the reinforcing fiber substrate in a state in which the reactivity is maintained. [0020] In the material for FRP molding of the present invention, the phenoxy resin (A) used as an essential component of the matrix resin composition is preferably solid at normal temperature and has a melt viscosity of 1×10 4 Pa at 220 ° C. . s the following. The melt viscosity is preferably from 1 × 10 2 to 6 × 10 3 Pa. s, more preferably 2 × 10 2 ~ 3 × 10 3 Pa. s. The melt viscosity exceeds 1 × 10 4 Pa. In the case of s, the fluidity of the resin during the forming process is deteriorated, so that the resin does not sufficiently travel into the fiber base material to cause voids, and the mechanical properties of the molded article are lowered. [0021] The phenoxy resin (A) is a thermoplastic resin obtained by a condensation reaction of a divalent phenol compound with an epihalohydrin or a polyaddition reaction of a divalent phenol compound with a bifunctional epoxy resin, which may be in a solvent or not. The solvent is obtained by a conventional method. The average molecular weight is usually 10,000 to 200,000, preferably 20,000 to 100,000, more preferably 30,000 to 80,000, in terms of mass average molecular weight (Mw). When the Mw is too low, the strength of the molded body is poor, and if it is too high, it is likely to be inferior in workability or workability. Further, Mw means a value measured by gel permeation chromatography and converted using a standard polystyrene calibration line. Further, the hydroxy group equivalent (g/eq) of the phenoxy resin (A) is usually from 50 to 1,000, preferably from 100 to 750, particularly preferably from 200 to 500. When the hydroxyl group equivalent is too low, the water absorption rate is increased by the increase of the hydroxyl group, so that there is a concern that the mechanical properties are lowered, and when the hydroxyl group equivalent is too high, the crosslinking density is insufficient to lower the heat resistance. The glass transition temperature (Tg) of the phenoxy resin (A) is preferably 65 ° C to 150 ° C or less, preferably 70 ° C to 100 ° C, more preferably 80 ° C to 100 ° C. When the glass transition temperature is lower than 65 ° C, the moldability is good, but the storage stability of the powder or the contact tackiness of the FRP molding material causes problems. When the temperature is higher than 150 ° C, the melt viscosity is also high to make the formability or the filling property to the fiber poor, and as a result, it is necessary to press-form at a higher temperature. Further, the glass transition temperature of the phenoxy resin was measured by a differential scanning calorimeter (DSC) at a temperature rise of 10 ° C / min in the range of 20 to 280 ° C, and the value calculated from the peak of the second scan. [0024] The phenoxy resin (A) is not particularly limited as long as it satisfies the above physical properties, but may be exemplified by bisphenol A type phenoxy resin (for example, PHENOTOTO YP-50, PHENOTOTO YP-made by Nippon Steel & Sumitomo Chemical Co., Ltd.) 50S, PHENOTOTO YP-55U), bisphenol F type phenoxy resin (such as PHENOTOTO FX-316 manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.), or copolymerized phenoxy resin of bisphenol A and bisphenol F (for example, new YP-70, manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd., and a special phenoxy resin (for example, YPB-43C, FX293, manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.), etc., may be used alone or in combination of two or more. [0025] The epoxy resin (B) can be blended with the phenoxy resin (A) in the matrix resin composition used in the FRP molding material of the present invention. By coexisting the epoxy resin (B), in addition to lowering the melt viscosity of the matrix resin composition, the impregnation property to the reinforcing fiber substrate can be improved, and the strength and physical properties of the cured product can be improved. In this case, the melt viscosity of the matrix resin composition basically depends on the melt viscosity of the phenoxy resin, but is affected by the blending amount of the epoxy resin or the type of the crosslinking agent. For example, when the blending amount of the epoxy resin is large, the melting period of the matrix resin composition is lowered. If the crosslinking agent is not suitable, the melt viscosity cannot be lowered due to rapid reaction, and therefore it is necessary to appropriately adjust. The epoxy resin (B) is preferably a bifunctional or higher epoxy resin, for example, a bisphenol A type epoxy resin (for example, EPOTOTO YD-011, EPOTOTO YD-7011, EPOTOTO YD-made by Nippon Steel & Sumitomo Chemical Co., Ltd.) 900), bisphenol F type epoxy resin (such as EPOTOTO YDF-2001 manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.), diphenyl ether type epoxy resin (for example, YSLV-80DE manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.) , tetramethyl bisphenol F type epoxy resin (for example, YSLV-80XY manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.), bisphenol thioether type epoxy resin (for example, YSLV-120TE manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.) Hydroquinone type epoxy resin (such as EPOTOTO YDC-1312 manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.), phenol novolac type epoxy resin (such as EPOTOTO YDPN-638 manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.), Neighbor A Phenolic novolac type epoxy resin (such as EPOTOTO YDCN-701, EPOTOTO YDCN-702, EPOTOTO YDCN-703, EPOTOTO YDCN-704 manufactured by Nippon Steel & Sumitomo Chemical Co., Ltd.), aralkyl naphthalene phenol novolac epoxy Resin (for example, ESN from Nippon Steel & Sumitomo Chemical Co., Ltd.) 355), a triphenylmethane type epoxy resin (for example, EPPN-502H by Nippon Kayaku Co., Ltd.), and the like, but is not limited thereto, and may be used in combination of two or more kinds. Further, in order to store the matrix resin composition as a powder, the epoxy resin (B) is preferably a solid at room temperature, preferably a melting point of 75 ° C to 145 ° C, and melting at 160 ° C. The viscosity is 1.0Pa. Crystalline epoxy resin below s. More than 1.0Pa. In the case of s, the matrix resin composition is inferior in filling property to the reinforcing fiber base material, and the obtained molded body is inferior in homogeneity. Further, since the crystalline epoxy resin has a melt viscosity much lower than that of the solid epoxy resin, the impregnation property of the matrix resin can be improved by blending the crystalline epoxy resin. Therefore, a high melt viscosity phenoxy resin can be used. [0027] The crosslinking agent (C) used in the present invention may be one having two or more functional groups reactive with the epoxy group of the hydroxy group of the phenoxy resin and the epoxy group of the epoxy resin, and is the above general formula. An anhydride represented by (1) to (3). Since one acid anhydride is hydrolyzed to produce two carboxyl groups, it is understood to have two such functional groups. Further, the acid anhydride as a crosslinking agent crosslinks the phenoxy resin three-dimensionally by forming an ester bond with the second-order hydroxyl group of the phenoxy resin. Therefore, unlike the strong crosslinking such as hardening of the thermosetting resin, the crosslinking can be solved by a hydrolysis reaction or the like, so that the recyclability does not hinder. [0028] The acid anhydride can be used as the crosslinking agent (C) if it is solid at normal temperature and has low sublimation property. However, in the present invention, it is aromatic four based on the viewpoint of imparting heat resistance to the molded product or increasing the crosslinking density. The carboxylic acid dianhydride is at least one aromatic tetracarboxylic dianhydride represented by the general formulae (1) to (3). Wherein X represents O, -CH 2 -, -C(CH 3 )-, -(Ph) m -, -Ph-CH 2 -Ph- or -Ph-C(CH 3 ) 2 -Ph-, Ph To stretch the phenyl group, m is an integer from 1 to 4. Wherein Y represents -(CH 2 ) m -, -(Ph) m -, -Ph-CH 2 -Ph- or -Ph-C(CH 3 ) 2 -Ph-, Ph is a phenylene group, m is An integer from 1 to 4. Further, in the description of X and Y, if -(Ph) m -, -Ph-CH 2 -Ph- or -Ph-C(CH 3 ) 2 -Ph- is represented by a structural formula, the following is true. The bonding bond is not limited to the alignment shown by the structural formula, but may be the ortho position. The crosslinking agent can dissolve the molten phenoxy resin and the epoxy resin to make the matrix resin composition transparent. , you can use it. [0029] The aromatic tetracarboxylic dianhydrides represented by the general formulas (1) to (3) are benzene oxygen which is not easily combined with the main component of the matrix resin composition because most of the crosslinking agent itself is melted by heat. Since the base resin or the epoxy resin is compatible, the crosslinking viscosity does not cause an increase in the melt viscosity from the low temperature. Therefore, since the crosslinking reaction starts after the matrix resin composition is melted to a sufficiently low viscosity during the molding process, the matrix resin is excellent in impregnation with the reinforcing fiber substrate, and the crosslinking reaction is not too fast or too insufficient. Since it is carried out, the foreign matter remains in the matrix resin in an unreacted state, and there is no problem that the mechanical strength of the molded article starting from the residual crosslinking agent (C) or the mechanical strength during heating is lowered. Further, the compatibility of the crosslinking agent (C) with the phenoxy resin (A) and the epoxy resin (B) can be visually observed by melting and kneading the matrix resin composition of the mixture at 200 ° C. The reaction product after cooling was evaluated for transparency. [0030] As such aromatic tetracarboxylic dianhydrides, for example, 4,4'-oxydiphthalic anhydride or 4,5'-oxydiphthalic anhydride, 5,5'-Asia Methyl bis(isobenzofuran-1,3-dione), 5,5'-isopropylidene bis(isobenzofuran-1,3-dione), ethylene glycol diphenyl trimellitic anhydride, Bis(1,3-dioxoisobenzofuran-5-carboxylic acid) tetramethylene, 4,5'-[1,4-phenylenebis(oxy)]bis(isobenzofuran- 1,3-diketone), 4,4'-(m-phenylene dioxy)bis(isobenzofuran-1,3-dione), 5,5'-[1,3-phenylene Bis(oxy)]bis(isobenzofuran-1,3-dione), 3,3'-(p-phenylenedioxy)diphthalic anhydride, 5,5'-[ 1,2-phenylphenylbis(oxy)]bis(isobenzofuran-1,3-dione), 4,4'-[2,1-phenylphenylbis(oxy)]bis (iso) Benzofuran-1,3-dione), 4,4'-(p-phenylenedioxy)diphthalic anhydride, 5,5'-[biphenyl-4,4'-diyl Bis(oxy)]bis(isobenzofuran-1,3-dione), 5,5'-[biphenyl-2,2'-diylbis(oxy)]bis(isobenzofuran- 1,3-diketone), bisphenol A, diphthalic anhydride, 2,2'-bis(4-phenyltrimethyleneoxy)biphenyl dianhydride, 2,2'-bis(4-hydroxyl Phenyl)propane diphenyl Ester-3,3',4,4'-tetracarboxylic dianhydride, bis(1,3-dioxoisobenzofuran-5-carboxylic acid) isopropylidene bis(4,1-phenylene) , 3,3'-diphenyl-4,4'-biphenol-bis(benzene trimellitic anhydride), etc., preferably selected from 4,4'-oxydiphthalic anhydride, ethylene As the crosslinking agent (C), at least one aromatic tetracarboxylic acid such as alcohol diphenyltricarboxylic anhydride or 4,4'-(1-methylethylidene)diphthalic anhydride. [0031] The reaction of the phenoxy resin (A), the epoxy resin (B), and the crosslinking agent (C) is carried out by making the hydroxyl group of the phenoxy resin (A) and the crosslinking agent (C) The esterification reaction of the acid anhydride group further crosslinks and hardens by reacting the carboxyl group formed by the esterification reaction with the epoxy group of the epoxy resin (B). The phenoxy resin crosslinked body can be obtained by the reaction of the phenoxy resin (A) and the crosslinking agent (C), but by coexisting the epoxy resin (B), the melt viscosity of the matrix resin composition can be reduced. In addition to the impregnation of the reinforcing fiber base material, it is preferable to use an FRP molded article which is excellent in the crosslinking reaction, the crosslinking density, and the mechanical strength. Further, in the present invention, the epoxy resin (B) is coexistent, but it is considered that the phenoxy resin (A) of the thermoplastic resin is used as a main component, and the esterification of the secondary hydroxyl group and the acid anhydride group of the crosslinking agent (C) is considered. The reaction is preferred. That is, the reaction of the acid anhydride used as the crosslinking agent (C) with the epoxy resin (B) takes time, so that the reaction with the hydroxy group of the phenoxy resin (A) is first caused, if the crosslinking agent (C) When the anhydride is deactivated, the reactivity with the epoxy resin (B) is greatly reduced. Therefore, the FRP molding material of the present invention is different from the usual FRP molding material which is mainly composed of an epoxy resin of a thermosetting resin, and the moldability or the physical properties of the FRP molded article can be maintained even after storage for a long period of time at room temperature. , excellent storage stability. Further, in the phenoxy resin composition of the present invention, a hardening accelerator (D) may be blended. The hardening accelerator (D) is not particularly limited as long as it is solid at room temperature and does not have sublimation properties, and examples thereof include a tertiary amine such as tri-ethylidene diamine, 2-methylimidazole, 2-phenylimidazole, and 2 An imidazole such as phenyl-4-methylimidazole, an organic phosphine such as triphenylphosphine or a tetraphenylboron salt such as tetraphenylphosphonium tetraphenylborate. These accelerators (D) may be used alone or in combination of two or more. Further, from the viewpoint of the production process of the present invention, it is preferred to use a hardening accelerator which is a solid imidazole latent catalyst having a catalytic activity temperature of 130 ° C or higher. Further, in the FRP molding material of the present invention, other thermoplastic resin powders such as poly may be blended in a range that does not impair the adhesion to the reinforcing fiber base material or the physical properties of the FRP molded body of the molded article. A powder of a vinyl chloride resin, a polyvinylidene chloride resin, a natural rubber, a synthetic rubber, or the like, or other additives such as various inorganic fillers, extender pigments, colorants, antioxidants, and ultraviolet rays preventive agents. [0034] The matrix resin composition of the FRP molding material of the present invention is promoted by hardening of a phenoxy resin (A), an epoxy resin (B), and a crosslinking agent (C) which are essential components, and if necessary. The agent (D) or the moisture-resistant pigment, the colorant, and other additives are pulverized to a specific size, and then mixed at a specific blending ratio, and the matrix resin micro-composite is attached to the reinforcing fiber substrate in a powder state. The matrix composition of the present invention is blended with the epoxy resin (B) in an amount of 5 to 85 parts by weight based on 100 parts by weight of the phenoxy resin (A). It is preferably from 9 to 83 parts by weight, more preferably from 10 to 70 parts by weight. When the blending amount of the epoxy resin exceeds 85 parts by weight, since it takes time to harden the epoxy resin, in addition to the difficulty in obtaining the strength required for demolding in a short time, the recovery property of FRP is also lowered. Further, when the blending amount of the epoxy resin (B) is less than 5 parts by weight, the effect of blending the epoxy resin cannot be obtained, and the cured product of the matrix resin composition hardly exhibits a Tg of 160 ° C or more. [0036] The matrix resin composition is solid at normal temperature, and its melting viscosity is 3,000 Pa at any temperature in the temperature range of 160 to 220 ° C. s below. 160 to 220 ° C is a temperature zone where hot press forming is usually performed. Preferably it is 2,900Pa. Below s, better is 2,800Pa. s. If the melt viscosity exceeds 3,000Pa. s, when the matrix resin composition is formed by hot pressurization, the impregnation of the reinforcing fiber base material is insufficient, and defects such as internal voids are generated, and the mechanical properties of the FRP are lowered. Further, when the phenolic resin (A) and the epoxy resin (B) having a melt viscosity in the matrix resin composition are reacted with the crosslinking agent (C), they are rapidly increased. Therefore, if the phenoxy resin (A) and the epoxy resin (B) do not melt sufficiently before starting the reaction with the crosslinking agent (C), the melt viscosity will not become 3,000 Pa. In the following, the impregnation of the matrix resin to the reinforcing fiber substrate is caused, and voids are generated in the molded body. Therefore, the melting point of the crosslinking agent (C) is desirably 150 ° C or more, preferably in the range of the molding temperature (160 to 220 ° C). The amount of the crosslinking agent (C) to be blended is usually in the range of from 0.6 to 1.3 mols per hydroxy group of the phenoxy resin (A), and preferably from 0.9 to 1.3 mols. 1.3 The range of the range of Moh, preferably in the range of 0.9 to 1.1 moles. When the amount of the acid anhydride group is too small, the reactive acid anhydride group is insufficient with respect to the second-order hydroxyl group of the phenoxy resin (A), so that the crosslinking density is low and the rigidity is poor, and when it is too large, the hydroxyl group of the phenoxy resin (A) is second. The acid anhydride group is excessive and the unreacted acid anhydride adversely affects the hardening property or the crosslinking density. Further, it is considered that the phenoxy resin is not directly crosslinked by the acid anhydride group (COOH) of the crosslinking agent, and the phenoxy resin is crosslinked by the epoxy resin, and two kinds of forms are present, and the acid anhydride of the crosslinking agent is presumed. The carboxyl group obtained by ring-opening of the acid group and the acid anhydride group is consumed by the hydroxyl group of the phenoxy resin and the epoxy group of the epoxy resin, and there is almost no carboxyl group remaining in the hardened material. [0038] In addition to the necessary components (A) to (C), when the hardening accelerator (D) is also used, the blending amount of (D) is relative to the phenoxy resin (A), the epoxy resin (B), and The total amount of the crosslinking agent (C) is 100 parts by weight, and is 0.1 to 5 parts by weight. The other additives are appropriately adjusted so as not to impair the adhesion of the matrix resin composition powder to the substrate or the properties of the molded article. Further, in the material for FRP molding of the present invention, it is desirable to add a flame retardant. The flame retardant is not particularly limited as long as it is solid at room temperature and does not sublimate, but it is preferably used as a non-halogen flame retardant based on environmental or health effects, for example, an inorganic flame retardant such as calcium hydroxide, Or a phosphorus-based flame retardant such as an ammonium phosphate or a phosphate compound, or a phosphorus-based flame retardant which is an inorganic compound, a nitrogen-containing flame retardant such as a triazine compound, or a bromine-based flame retardant such as a brominated phenoxy resin. Among them, a brominated phenoxy resin or a phosphorus-containing phenoxy resin can be preferably used because it can be used as a flame retardant and a matrix resin. The blending amount of the flame retardant is appropriately selected depending on the type of the flame retardant or the degree of flame retardancy desired, but it is preferably in the range of 0.01 to 10 parts by weight based on 100 parts by weight of the matrix resin composition. The degree of adhesion of the resin composition or the physical properties of the FRP molded article is blended. In the method for producing a FRP molding material according to the present invention, each component constituting the matrix resin composition is attached to the reinforcing fiber substrate as a fine powder. Therefore, each component is pulverized into a fine powder. This pulverization is preferably carried out using a pulverizing mixer such as a low-temperature drying pulverizer (centrifugal drying mill), but is not limited thereto. Further, in the case of pulverization, the components may be pulverized and mixed, or may be pulverized by mixing the components in advance, but it is preferably the former. In this case, the pulverization conditions may be set so that each of the fine powders has an average particle diameter to be described later. As the powder thus obtained, the average particle diameter is from 10 to 100 μm, preferably from 40 to 80 μm, more preferably from 40 to 50 μm. When the average particle diameter exceeds 100 μm, when the powder is adhered to the reinforcing fiber base material in the powder coating in the electrostatic field, the energy when the resin collides with the fiber becomes large, and the adhesion rate to the reinforcing fiber base material is lowered. When the particle size is less than 10 μm, the particles are scattered by the air current to lower the adhesion efficiency, and the fine powder resin floating in the air may cause a deterioration in the working environment. In this case, the average particle diameter of the phenoxy resin (A) and the epoxy resin (B) powder is preferably from 1 to 1.5 times the average particle diameter of the crosslinking agent (C). By making the particle diameter of the crosslinking agent (C) powder finer than the powders of the phenoxy resin (A) and the epoxy resin (B), the crosslinking agent (C) can be adhered to the inside of the reinforcing fiber substrate. Further, the crosslinking agent (C) does not exist around the particles of the components (A) and (B), and the crosslinking reaction can be surely carried out. The FRP molding material of the present invention is obtained by adhering a powder of a matrix resin composition to a reinforcing fiber substrate by a powder coating method. The powder coating method includes a flow coating method using a fluidized bed and an electrostatic coating method using an electrostatic field. Although any method can be used in the present invention, it is preferably used based on adhesion uniformity to a reinforcing fiber substrate. Electrostatic coating method for electrostatic fields. The adhesion amount of the matrix resin composition to the reinforcing fiber substrate is applied so that the resin ratio (RC) is 20 to 50% by weight, but it is preferably 25% to 40%, more preferably 25 to 30%. When the resin adhesion rate exceeds 50%, the stretching of FRP. The mechanical properties such as the bending elastic modulus are lowered. When the amount of the resin adhered is extremely reduced, the impregnation of the base resin into the interior of the substrate is insufficient, and both the thermal properties and the mechanical properties are lowered. [0043] The powder of the matrix resin composition coated with the powder is fixed to the reinforcing fiber substrate by heating and melting, but may be cooled and coated by applying the powder, followed by heating and heating. Any of the thermal coatings in which the reinforcing fibers are applied to the powder and fused. By this heating and melting, the matrix resin on the surface of the reinforcing fiber base material is melted to improve the adhesion to the substrate, and the coated resin powder is prevented from falling off. However, in the obtained FRP material, the matrix resin concentrates on the surface of the reinforcing fiber substrate, and cannot travel to the inside of the reinforcing fiber substrate as in the case of the molded body after the heat and pressure molding. Further, the heating time after the powder coating is not particularly limited as long as the matrix resin composition of the FRP molding material can maintain the range of fluidity and reactivity, but it is usually preferably 1 to 2 minutes. That is, by performing heat treatment much shorter than the molding time, the phenoxy resin or the epoxy resin is fixed to the reinforcing fiber substrate by thermal fusion without reacting the crosslinking agent with the resin to prevent powder from falling off. The melting temperature is 150 to 240 ° C, preferably 160 to 220 ° C, more preferably 180 to 200 ° C. When the melting temperature exceeds the upper limit, there is a possibility that the curing reaction proceeds, and when the temperature is lower than the lower limit, the thermal fusion is insufficient, and the matrix resin is powdered or dropped during the treatment of the FRP molding material. [0044] The reinforcing fiber substrate may be carbon fiber, glass fiber, polyarmine fiber, boron fiber, alumina fiber, mineral fiber, tantalum carbide fiber, etc., but it is preferably required to have conductivity when using electrostatic coating. For carbon fiber. Further, the form of the reinforcing fiber base material is not particularly limited. For example, a single-directional material, a plain weave or a woven fabric, a three-dimensional cloth, a chopped strand mats, and a plurality of filaments may be used. Into the vine, or non-woven cloth. These reinforcing fiber base materials may be used alone or in combination of two or more. The material for FRP molding of the present invention thus produced can be easily produced by laminating, heating, and pressurization. Further, a metal foil such as aluminum or stainless steel may be laminated on the interlayer or the outermost layer during lamination. The FRP molding material of the present invention can be simultaneously subjected to cross-linking and hardening of the forming and matrix resin by press molding by hot pressurization. The molding using the FRP molding material can be carried out by various molding methods such as autoclave molding or hot press molding using a metal mold by appropriately selecting the size or shape of the intended FRP molded product. . The forming temperature is, for example, 150 to 240 ° C, preferably 160 ° C to 220 ° C, and more preferably 180 ° C to 200 ° C. Further, when the molding temperature exceeds the upper limit temperature of the above range, excessive heat is applied to cause decomposition of the resin, and when the temperature is lower than the lower limit temperature, the impregnation property of the fiber is deteriorated due to an increase in the melt viscosity of the matrix resin composition. . In addition, the molding time is usually 30 to 60 minutes, but even if it is a short time of about 10 minutes, it is also possible to use a secondary hydroxyl group of a phenoxy resin (A) as a main component and a crosslinking agent (C). The reaction is carried out to obtain the strength of demolding. However, in order to complete the hardening reaction of the epoxy resin (B), it is preferably cured at a temperature of, for example, 200 to 250 ° C for about 30 to 60 minutes. The FRP molding material produced by the crosslinking treatment of the matrix resin composition by the secondary hydroxyl group of the phenoxy resin causes the heat resistance to be greatly increased before the molding, and the formation of a Tg of 160° C. or higher is obtained. Things. Since the softening point of the matrix resin composition is within about -25 ° C from Tg, for example, in hot press forming using a metal mold, the release temperature of the molded article from the metal mold is from the Tg of the hardened material of the matrix resin composition. A range of -30 ° C or less is possible, and it is preferred that the cured product is from Tg - 35 ° C or less, more preferably from Tg - 40 ° C or less. Further, when the mold release temperature exceeds the upper limit temperature of the above range, the shape cannot be maintained, and when the mold release temperature is too low, the time required for cooling becomes long, so that the station time (tact time) becomes long and the productivity is lowered. Further, the softening point indicates the temperature at which the storage elastic modulus (E') of the cured matrix resin is attenuated by the DMA. [0047] The cured product of the fiber-reinforced plastic molding material of the present invention is obtained by heat-curing the FRP molding material, and is a developed one. The cured product includes a cured product of a matrix resin and a reinforcing fiber base material in the fiber-reinforced plastic molding material, and these are strongly bonded to impart characteristics such as specific strength. Further, the glass transition temperature of the crosslinked cured product of the matrix resin composition is preferably 160 ° C or higher. [0048] The method for producing a fiber-reinforced plastic molded article of the present invention is a method in which the fiber-reinforced plastic molding material is heated, pressurized, and cured. [Examples] The present invention will be specifically described below by showing examples, but the present invention is not limited to those described in the examples. [0050] Materials used in the examples and comparative examples are as follows. Phenoxy Resin (A) (A-1) PHENTOTO YP-50S (Nippon Steel Sumikin Chemical Co., Ltd. bisphenol A type, Mw = 40,000, hydroxyl equivalent = 284), melt viscosity at 200 ° C =3,000Pa. s, glass transition temperature (Tg) = 83 ° C Epoxy resin (B) (B-1): YSLV-80XY (Nippon Steel Sumikin Chemical Co., Ltd. made tetramethyl bisphenol F type, epoxy equivalent = 192, Melting point: 72 ° C) Crosslinking agent (C) (C-1): ethylene glycol trimellitic anhydride (anhydride equivalent: 207, melting point: 160 ° C, TEMG) (C-2): 4,4'-oxydi-n-alloy Phthalic anhydride (anhydride equivalent: 153, melting point: 225 ° C, OPDA) (C-3): bisphenol A, diphthalic anhydride (Acid anhydride equivalent: 260, melting point: 184 ° C, BisDA manufactured by SABIC Co., Ltd.) (C-4): 4,4'-diphthalic anhydride (anhydride equivalent: 147, melting point: 229 ° C, BPDA) (C-5) ): 3,3',4,4'-benzophenonetetracarboxylic dianhydride (anhydride equivalent: 161, melting point: 218 ° C, BTDA) (C-6): 3,3',4,4'- Diphenylphosphonium tetracarboxylic dianhydride (anhydride equivalent: 179, melting point: ≧287 ° C, DSDA) [0052] The test and measurement methods of various physical properties are as follows. [0053] The melt viscosity of the melt-viscosity matrix resin composition or the like is a rheometer (manufactured by Anton Paar Co., Ltd.), and the sample size is 4.3 cm 3 with a parallel plate, and the temperature is raised at 50° C./min. Load deformation: 5% of the conditions, the melt viscosity of 160 ° C was measured. [0054] The average particle size of the average particle size matrix resin composition powder or the like is laser diffraction. A scattering type particle size distribution measuring apparatus (MICROTRACK MT3300EX, manufactured by Nikkiso Co., Ltd.) was used to measure the average particle diameter (D50) on a volume basis. Compatibility of Resin (A), (B) and Crosslinking Agent (C) (Transparency) The crosslinking agent (C) is blended in the phenoxy resin (A) and the epoxy resin (B). The matrix resin composition was melted at 200 ° C and kneaded, and the reaction product after cooling was visually observed to evaluate transparency. [0056] The touch-sensitive property of the pre-formed sheet was contacted with the surface of the obtained FRP-forming material by a finger, and the non-sticking property was determined to be acceptable, and it is indicated as ○ in Table 1. The resin ratio (RC: %) was calculated from the weight (W1) of the carbon fiber cloth before the adhesion of the matrix resin composition and the weight (W2) of the FRP molding material after the resin composition was adhered, using the following formula. Resin ratio (RC:%)=(W2-W1)/W2×100 W1: Weight of reinforcing fiber before attachment of matrix resin composition W2: Weight of FRP molding material after attachment of matrix resin composition [0058] Glass transition temperature (Tg), resin softening temperature Test piece having a thickness of 2 mm, a width of 10 mm, and a length of 10 mm, using a dynamic viscoelasticity measuring device (DMA 7e, manufactured by Perkin Elmer Co., Ltd.) at a temperature rise of 5 ° C / min, at 25 to 250 ° C The range was measured, and the obtained maximum peak of tan δ was set as the glass transition point. Further, the resin softening temperature was set to the temperature of the turning point of the same test piece in which the storage elastic modulus (E') measured by DMA was attenuated. It indicates the mold release temperature after the form hardening. [0059] The material for mechanical physical FRP molding was superposed on 13 sheets of Teflon (registered trademark) sheet, and heated at 200 ° C for 10 minutes to prepare an FRP laminate, and then dried in an oven. After curing in an hour, the mechanical properties (bending modulus, bending strength) of the obtained FRP laminate were measured based on the bending test method of the fiber-reinforced plastic according to JIS K 7074:1988. [0060] The resin impregnated FRP molding material was superposed on 13 sheets of Teflon sheet, and pressed at 5 MPa for 5 minutes by a press machine heated to 200 ° C to form a laminate, and then cured in an oven for 1 hour, and used. The diamond cutter cuts out a few pieces of 10mm square pieces. After the cut piece was polished with a water-resistant abrasive paper of #1000 or more, the cut surface was observed by an optical microscope to confirm the presence or absence of a hole. [0061] The material for FRP molding is stored at room temperature for 3 months. The FRP molding material is superimposed on the Teflon sheet by 13 sheets, and the press is heated to 200 ° C to pressurize at 5 MPa. The laminate was produced in minutes and cured in an oven for 1 hour to evaluate thermal properties or mechanical properties. When compared with the laminate produced 3 months ago, the physical property error was within the range of ±10%, which was acceptable, and is indicated as ○ in Table 1. [0062] The long-term heat resistance test of CFRP was carried out in the same manner as the test piece for the measurement of mechanical properties, and was maintained at a temperature of 100 ° C for 500 hours, and then subjected to a bending test method of fiber-reinforced plastic according to JIS K 7074:1988. Mechanical strength test. [Example 1] (A-1) as the phenoxy resin (A), (B-1) as the epoxy resin (B), and (C-1) as the crosslinking agent (C) The pulverized and classified powder having an average particle diameter D50 of 80 μm (the average particle diameters of A, B, and C are substantially the same) is dry blended in the proportion (parts by weight) shown in Table 1, and is charged in an electrostatic field. A condition of 70 kV and a blown air pressure of 0.32 MPa was applied to a fiber-dyed woven fiber substrate made of carbon fiber (STANDARD Modulus type HST 403K, manufactured by TOHO TENAX Co., Ltd.). Subsequently, the resin was heat-fused at 170 ° C for 1 minute in an oven to thermally fuse the resin to obtain a FRP molding material. The resin ratio (RC) of the obtained FRP molding material was 27%. Various physical properties were measured about the FRP molding material and the FRP cured product thus obtained. These results are shown in Table 1. [0064] Examples 2, 3 and Comparative Examples 1 to 3 As the crosslinking agent (C), (C-2), (C-3), (C-4), (C) were used instead of (C-1). In the same manner as in Example 1, except for (C-6), a material for FRP molding was obtained, and an FRP laminate was obtained, and various physical properties were evaluated. The results are also shown in Table 1. Further, regarding the bending elastic modulus, the bending strength, and the long-term heat resistance of Comparative Example 3, the matrix resin was brittle and could not be measured. [0065] From the results obtained in Table 1, it was found that the fine powder of the matrix resin composition using C-1, C-2, and C-3 as the crosslinking agent (C) was adhered to the FRP molding material of the reinforcing fiber substrate. CFRP exhibits excellent heat resistance of Tg of 160 ° C or more, and since the matrix resin composition has a low melt viscosity, it has good impregnation properties to the reinforcing fiber base material and exhibits high mechanical strength. Further, since the crosslinking agent has good compatibility with the phenoxy resin and the epoxy resin, the reactivity is good, and since it does not remain as a solid matter, the mechanical strength is lowered even if it is exposed to heating conditions of 100 ° C for a long period of time. . In the FRP molding material of the present embodiment, the FRP molded article having high heat resistance and mechanical properties at room temperature and heating can be obtained, and therefore it is excellent as a material for FRP molding. [Industrial use field] The fiber reinforced plastic molding material of the present invention is used as a fiber reinforced plastic (FRP) material, and can be used in a car body or a body of a transportation machine such as an automobile or an airplane machine, a notebook personal computer or It is used in a wide range of fields such as the frame of electronic devices for tablet computers, arms for industrial robots, reinforcing materials for building structures, sports and leisure fields for fishing rods or road bicycles.