TW201418308A - Epoxy resin, epoxy resin composition, method for curing same, and cured product thereof - Google Patents

Epoxy resin, epoxy resin composition, method for curing same, and cured product thereof Download PDF

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TW201418308A
TW201418308A TW102124522A TW102124522A TW201418308A TW 201418308 A TW201418308 A TW 201418308A TW 102124522 A TW102124522 A TW 102124522A TW 102124522 A TW102124522 A TW 102124522A TW 201418308 A TW201418308 A TW 201418308A
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epoxy resin
resin composition
temperature
cured product
phenol
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TW102124522A
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Koichiro Ogami
Ken Hirota
Hisashi Yamada
Hideyasu Asakage
Masashi Kaji
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Nippon Steel & Sumikin Chem Co
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/02Polycondensates containing more than one epoxy group per molecule
    • C08G59/04Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof
    • C08G59/06Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols
    • C08G59/063Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols with epihalohydrins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/20Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the epoxy compounds used
    • C08G59/32Epoxy compounds containing three or more epoxy groups
    • C08G59/3218Carbocyclic compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/40Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the curing agents used
    • C08G59/62Alcohols or phenols
    • C08G59/621Phenols
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G59/00Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
    • C08G59/18Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
    • C08G59/68Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the catalysts used
    • C08G59/686Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the catalysts used containing nitrogen
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L23/00Details of semiconductor or other solid state devices
    • H01L23/28Encapsulations, e.g. encapsulating layers, coatings, e.g. for protection
    • H01L23/29Encapsulations, e.g. encapsulating layers, coatings, e.g. for protection characterised by the material, e.g. carbon
    • H01L23/293Organic, e.g. plastic
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L2924/00Indexing scheme for arrangements or methods for connecting or disconnecting semiconductor or solid-state bodies as covered by H01L24/00
    • H01L2924/0001Technical content checked by a classifier
    • H01L2924/0002Not covered by any one of groups H01L24/00, H01L24/00 and H01L2224/00

Abstract

Provided is an epoxy resin cured product that, whether used for lamination, molding, or casting, has excellent high heat resistance, high-temperature and long-term pyrolysis stability, and fluidity, and that is useful in the sealing of electrical and electronic parts, for circuit substrate materials, and the like. Provided are: an epoxy resin containing at least 10% of a polymer represented by general formula (2), wherein n is 1 or greater; an epoxy resin composition containing the epoxy resin, a phenolic curing agent, a curing catalyst, and an inorganic filler; and a cured product thereof. Here, R is a hydrogen atom or a C1-6 hydrocarbon group, and G is a glycidyl group.

Description

環氧樹脂、環氧樹脂組成物、環氧樹脂組成物之硬化方法及硬化物 Epoxy resin, epoxy resin composition, hardening method of epoxy resin composition and hardened material

本發明係關於耐熱性、熱分解安定性及流動性優異,作為密封用之優異環氧樹脂、環氧樹脂組成物、其硬化方法及硬化物。 The present invention relates to an excellent epoxy resin, an epoxy resin composition, a curing method, and a cured product which are excellent in heat resistance, thermal decomposition stability, and fluidity.

環氧樹脂已使用於工業上廣泛之用途中,但其要求性能近年來越來越高度化。其中,近年開發所進展之功率裝置中,要求裝置之功率密度進一步提高,其結果,作動時之晶片表面溫度亦達250℃,而期望開發出可耐受該溫度之密封材料。 Epoxy resins have been used in a wide range of applications in the industry, but their performance has been increasing in recent years. Among them, in the development of power devices in recent years, the power density of the device is required to be further increased. As a result, the surface temperature of the wafer at the time of actuation is also 250 ° C, and it is desired to develop a sealing material which can withstand the temperature.

其中,作為耐熱性優異之環氧樹脂組成物,已知有使用具有四苯基乙烷構造之環氧樹脂者,例如,專利文獻1中顯示以四苯基乙烷型環氧樹脂與多元酚樹脂硬化劑作為必要成分之環氧樹脂組成物,且揭示耐熱性優異之環氧樹脂硬化物。另外,專利文獻2中揭示使用四苯基乙烷型環氧樹脂與酸酐硬化劑之耐熱性優異之環氧樹脂組成物及硬化物。然而,使用此四苯基乙烷型環氧樹脂時, 藉由通常之成形方法亦無法獲得玻璃轉移溫度為230℃左右之硬化物,其中在使用酚樹脂硬化劑時,僅能獲得200℃以下之玻璃轉移溫度之硬化物。因此,會有無法獲得滿足耐受高如250℃之作動溫度之用於高耐熱性功率裝置之密封材料特性之問題。 Among them, as an epoxy resin composition excellent in heat resistance, an epoxy resin having a tetraphenylethane structure is known. For example, Patent Document 1 shows a tetraphenylethane type epoxy resin and a polyhydric phenol. The resin hardener is an epoxy resin composition which is an essential component, and an epoxy resin cured product excellent in heat resistance is disclosed. Further, Patent Document 2 discloses an epoxy resin composition and a cured product which are excellent in heat resistance of a tetraphenylethane type epoxy resin and an acid anhydride curing agent. However, when using this tetraphenylethane type epoxy resin, A cured product having a glass transition temperature of about 230 ° C cannot be obtained by a usual molding method, and in the case of using a phenol resin hardener, only a cured product having a glass transition temperature of 200 ° C or less can be obtained. Therefore, there is a problem that the characteristics of the sealing material for a high heat-resistant power device satisfying the operating temperature of a high resistance such as 250 ° C cannot be obtained.

另外,耐受在高溫下之實際用時,不僅耐熱性指標的玻璃轉移溫度具重要性,高溫使用時之開始分解溫度也相當重要,故要求與玻璃轉移溫度同樣高之開始分解溫度之材料。 In addition, when it is practically used at a high temperature, not only the glass transition temperature of the heat resistance index is important, but also the decomposition temperature at the time of high temperature use is important, and therefore a material having a decomposition temperature higher than the glass transition temperature is required.

[先前技術文獻] [Previous Technical Literature]

[專利文獻1]特開平9-3162號公報 [Patent Document 1] JP-A-9-3162

[專利文獻2]特開平2-219812號公報 [Patent Document 2] JP-A-2-219812

本發明之目的係提供一種在層合、成形、注模、接著等之用途中,高耐熱性、高溫長期熱分解安定性優異,並且流動性亦優異之於電氣.電子零件類之密封、電路基板材料等中有用之環氧樹脂硬化物。 An object of the present invention is to provide a high heat resistance, a high temperature, a long-term thermal decomposition stability, and an excellent fluidity in electrical conductivity, such as lamination, molding, injection molding, and the like. A cured epoxy resin useful for sealing electronic components and circuit board materials.

本發明係關於一種以下述通式(2)表示之環氧樹脂, The present invention relates to an epoxy resin represented by the following general formula (2),

(在此,R獨立地表示氫原子或碳數1~6之烴基,G表示環氧丙基,n為重複數,包含10%以上n為1以上之多聚物)。 (here, R independently represents a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms, G represents a glycidyl group, and n is a repeating number, and 10% or more of n is a polymer having 1 or more).

另外,本發明係關於一種環氧樹脂,其特徵 係使以下述通式(1)表示,且以膠體滲透層析所測定之面積%中n=1以上之成分為10%以上之多元羥基化合物與表氯醇反應而得。 In addition, the present invention relates to an epoxy resin, the characteristics of which It is obtained by reacting a polyhydric hydroxy compound having 10% or more of a component having n = 1 or more in the area % measured by colloidal permeation chromatography with epichlorohydrin, which is represented by the following general formula (1).

該環氧樹脂較好為以上述通式(2)表示之環氧樹脂,較好包含10%以上之n為1以上之多聚物。 The epoxy resin is preferably an epoxy resin represented by the above formula (2), and preferably contains 10% or more of a polymer in which n is 1 or more.

(其中,R獨立地表示氫原子或碳數1~6之烴基,G表示環氧丙基,n表示重複數)。 (wherein R independently represents a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms, G represents a glycidyl group, and n represents a repeating number).

另外,本發明係關於一種環氧樹脂組成物,其特徵係含有上述之環氧樹脂、酚系硬化劑、硬化觸媒及無機填充劑。 Further, the present invention relates to an epoxy resin composition characterized by comprising the above epoxy resin, a phenolic curing agent, a curing catalyst, and an inorganic filler.

其中,硬化觸媒較好為咪唑類、有機膦類、或胺類所組成群組選出之至少1種,更好顯示出在利用DSC,於升溫速度10℃/分鐘條件下測定環氧樹脂時顯示發熱峰高點為150℃以上之硬化性能者。 Wherein, the hardening catalyst is preferably at least one selected from the group consisting of imidazoles, organic phosphines, or amines, and more preferably exhibits the use of DSC to measure the epoxy resin at a heating rate of 10 ° C /min. It shows the hardening performance at a high point of 150 °C or higher.

另外,本發明係關於一種環氧樹脂組成物之硬化方法,其特徵係使上述環氧樹脂組成物於100℃~200℃成形後,於200℃~300℃進行後硬化(postcure),及關於以上述硬化方法之硬化條件下硬化獲得之環氧樹脂硬化物。該環氧樹脂硬化物適於半導體密封材用。再者,本發明係關於一種半導體裝置,其特徵係以上述環氧樹脂硬化物密封半導體元件而成。 Further, the present invention relates to a method for curing an epoxy resin composition, characterized in that the epoxy resin composition is formed at 100 ° C to 200 ° C and then post-cured at 200 ° C to 300 ° C, and The cured epoxy resin obtained by hardening under the hardening conditions of the above hardening method. The epoxy resin cured product is suitable for use in a semiconductor sealing material. Furthermore, the present invention relates to a semiconductor device characterized by sealing a semiconductor element with the cured epoxy resin.

若使本發明之環氧樹脂組成物加熱硬化,則可成為環氧樹脂硬化物,該硬化物可獲得高耐熱性、高溫長期熱分解安定性、高流動性等方面優異者,可較好地使用於電氣.電子零件類之密封、回路基板材料等之用途中。 When the epoxy resin composition of the present invention is heat-cured, it can be an epoxy resin cured product, and the cured product can be excellent in high heat resistance, high-temperature long-term thermal decomposition stability, high fluidity, and the like. Used in electrical. In the use of electronic component seals, circuit substrate materials, etc.

圖1為合成例1所得之酚樹脂之GPC圖譜。 Fig. 1 is a GPC chart of the phenol resin obtained in Synthesis Example 1.

圖2為合成例2所得之環氧樹脂之GPC圖譜。 2 is a GPC chart of the epoxy resin obtained in Synthesis Example 2.

圖3為合成例3所得之酚樹脂之GPC圖譜。 Fig. 3 is a GPC chart of the phenol resin obtained in Synthesis Example 3.

圖4為合成例4所得之環氧樹脂之GPC圖譜。 4 is a GPC chart of the epoxy resin obtained in Synthesis Example 4.

圖5為合成例5所得之酚樹脂之GPC圖譜。 Fig. 5 is a GPC chart of the phenol resin obtained in Synthesis Example 5.

圖6為合成例6所得之環氧樹脂之GPC圖譜。 Fig. 6 is a GPC chart of the epoxy resin obtained in Synthesis Example 6.

圖7為合成例7所得之酚樹脂之GPC圖譜。 Fig. 7 is a GPC chart of the phenol resin obtained in Synthesis Example 7.

圖8為合成例8所得之環氧樹脂之GPC圖譜。 Fig. 8 is a GPC chart of the epoxy resin obtained in Synthesis Example 8.

以下,詳細說明本發明。 Hereinafter, the present invention will be described in detail.

本發明之環氧樹脂係以上述通式(2)表示之可藉由使以上述通式(1)表示之多元羥基化合物與表氯醇反應而製造。而且,該多元羥基化合物可藉由使酚與乙二醛(glyoxal)反應而製造。 The epoxy resin of the present invention can be produced by reacting the polyvalent hydroxy compound represented by the above formula (1) with epichlorohydrin, represented by the above formula (2). Moreover, the polyvalent hydroxy compound can be produced by reacting a phenol with glyoxal.

通式(1)及通式(2)中,相同符號具有相同意義,R獨立地表示氫原子或碳數1~6之烴基。較好,R為氫原子或碳數1~4之烷基。n為重複數,通常係n為不同的成分之混合物,但較好為由0~10之成分所成。而且,10%以上較好為n=1以上之多聚物。該n之%係以膠體滲透層析(GPC)所測定之面積%,n為1以上之多聚物成分之面積%較好為10%以上。 In the general formulae (1) and (2), the same symbols have the same meaning, and R independently represents a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms. Preferably, R is a hydrogen atom or an alkyl group having 1 to 4 carbon atoms. n is a repeating number, and usually n is a mixture of different components, but is preferably composed of components of 0 to 10. Further, 10% or more is preferably a polymer having n = 1 or more. The % of n is an area % measured by colloidal permeation chromatography (GPC), and an area % of a polymer component having n of 1 or more is preferably 10% or more.

過去,一般所製造之n=0之4官能之上述多元羥基化合物係相對於乙二醛使用大為過量之酚化合物而 得。酚化合物與乙二醛之反應中酚化合物相對於乙二醛之使用量並無限制,乙二醛之使用量相對於酚化合物1莫耳為0.02~0.2莫耳,較好為0.04~0.1莫耳。乙二醛之使用量多於0.2莫耳時,多元羥基化合物及由其所製造之環氧樹脂之軟化點變高而妨礙成形作業性,少於0.02莫耳時n=0體的生成變多,並且反應結束後除去過量之酚之量變多,工業上較不佳。使本發明之成為含多聚物之環氧樹脂的原料之多元羥基化合物係n為1以上之多聚物成分之面積%為10%以上,其可藉由調整酚化合物與乙二醛之莫耳比而成為期望之多聚物含量。 In the past, the above-mentioned polyhydric hydroxy compound having a 4-functionality of n=0 which is generally produced is a large excess of a phenol compound with respect to glyoxal. Got it. There is no limitation on the amount of the phenol compound to be used in the reaction of the phenol compound with the glyoxal. The amount of the glyoxal used is 0.02 to 0.2 mol, preferably 0.04 to 0.1 mol, relative to the phenol compound. ear. When the amount of glyoxal used is more than 0.2 mol, the softening point of the polyvalent hydroxy compound and the epoxy resin produced therefrom becomes high, which hinders the forming workability, and the formation of n=0 body becomes more than 0.02 mol. And the amount of excess phenol removed after the end of the reaction becomes large, which is industrially unsatisfactory. The area % of the polymer component in which the polyvalent hydroxy compound n of the polymer-containing epoxy resin of the present invention is 1 or more is 10% or more, which can be adjusted by adjusting the phenol compound and the glyoxal The ear ratio becomes the desired polymer content.

通常,該反應係在習知之無機酸、有機酸等 酸觸媒存在下進行。作為此酸觸媒列舉為例如鹽酸、硫酸、磷酸等無機酸,或甲酸、草酸、三氟乙酸、對-甲苯磺酸等有機酸,或氯化鋅、氯化鋁、氯化鐵、三氟化硼等之路易斯酸,或活性白土、二氧化矽-氧化鋁、沸石等固體酸等。 Usually, the reaction is in the conventional inorganic acid, organic acid, etc. It is carried out in the presence of an acid catalyst. Examples of the acid catalyst include inorganic acids such as hydrochloric acid, sulfuric acid, and phosphoric acid, or organic acids such as formic acid, oxalic acid, trifluoroacetic acid, and p-toluenesulfonic acid, or zinc chloride, aluminum chloride, iron chloride, and trifluorochloride. A Lewis acid such as boron or a solid acid such as activated clay, ceria-alumina or zeolite.

通常,該反應係於10~250℃進行1~20小 時。再者,反應時之溶劑較好使用例如甲醇、乙醇、丙醇、丁醇、乙二醇、甲基溶纖素、乙基溶纖素、二乙二醇二甲醚(diglyme)、三乙二醇二甲醚等醇類,或苯、甲苯、氯苯、二氯苯等芳香族化合物等。尤其就溶解性之觀點而言,以乙基溶纖素、二乙二醇二甲醚、三乙二醇二甲醚較佳。反應結束後,所得多元羥基樹脂亦可藉由減壓餾除、水洗或在弱溶劑中再沉澱等方法去除溶劑,但亦可殘留溶 劑直接使用作為環氧化反應之原料。 Usually, the reaction is carried out at 10~250 °C for 1~20 small Time. Further, the solvent for the reaction is preferably used, for example, methanol, ethanol, propanol, butanol, ethylene glycol, methyl cellosolve, ethyl cellosolve, diethylene glycol dimethyl ether (diglyme), triethyl ethane. An alcohol such as diol dimethyl ether or an aromatic compound such as benzene, toluene, chlorobenzene or dichlorobenzene. Particularly, from the viewpoint of solubility, ethyl cellosolve, diethylene glycol dimethyl ether, and triethylene glycol dimethyl ether are preferred. After the reaction is completed, the obtained polyhydric hydroxy resin may be removed by vacuum distillation, washing with water or reprecipitation in a weak solvent, but may be dissolved. The agent is used directly as a raw material for the epoxidation reaction.

因此製造之多元羥基化合物係以上述通式(1) 表示者,以GPC測定之面積%中,n=1以上之成分為10%以上,較好為11%以上,更好為12%以上。且,多聚物之比率變多時,使用其所得之環氧樹脂之黏度增加而使成形性降低,故n=1以上之成分較好為60%以下,更好為50%以下,最好為40%以下。又,平均重複數n(數平均)為0~5,但係調整為n=1以上之成分含10%以上。因此,n約成為0.10以上。 The polyhydroxy compound thus produced is of the above formula (1) In the area % measured by GPC, the component of n = 1 or more is 10% or more, preferably 11% or more, more preferably 12% or more. Further, when the ratio of the polymer is increased, the viscosity of the epoxy resin obtained by the use is increased to lower the moldability. Therefore, the component of n=1 or more is preferably 60% or less, more preferably 50% or less, and most preferably It is 40% or less. Further, the average number of repetitions n (number average) is 0 to 5, but the composition adjusted to n = 1 or more contains 10% or more. Therefore, n is approximately 0.10 or more.

本發明之環氧樹脂係以通式(2)表示之多聚物 混合物中主要以n=0成分之4官能環氧化合物作為主成分之環氧樹脂。以含10%以上之n=1以上之成分的多元羥基化合物作為原料使用時,環氧化步驟中,除了殘留未反應物之情況等以外,由於n未變化,故可認為成為與原料相同之n之含有率。本發明之環氧樹脂由於含以次甲基(methine)鏈鍵結之多聚物成分,其原理雖尚不清楚,但推測係相對地交聯較密,結果認為為熱分解安定性優異者。 The epoxy resin of the present invention is a polymer represented by the general formula (2) An epoxy resin having a 4-functional epoxy compound having a n=0 component as a main component in the mixture. When a polyvalent hydroxy compound containing 10% or more of n = 1 or more components is used as a raw material, in the epoxidation step, since n is not left, the n is not changed, so it is considered to be the same as the raw material. The content rate. Although the epoxy resin of the present invention contains a polymer component bonded by a methine chain, the principle is not clear, but it is presumed that the crosslinking is relatively dense, and the result is considered to be excellent in thermal decomposition stability. .

亦即,通式(2)之環氧樹脂中,n=0(4官能)成 分之比例增加時,乙烯單位與苯基環氧丙醚單位最接近於1:4。另一方面,認為使用更高官能成分的n=1(7官能)及n=2(10官能)成分之比例較高之多元羥基化合物時,上述比成為2:7及3:10,且交聯密度更密,藉由環氧丙醚單位相對較少而可獲得熱安定優異之硬化物。且,認為增加多官能成分時,關於與硬化劑之反應中藉由使硬化物 之交聯密度增加,亦可成為熱安定性更優異之硬化物。然而,增加n=5以上成分時,由於分子量變高,故有流動性或成形加工性變差之傾向。基於該理由,n係0~10之範圍之數,包含n=0,n之平均(數平均)較好為0.1~4之範圍。此n由於大致繼承作為原料使用之多元羥基化合物之n,故n之調整係藉由調整多元羥基化合物之n而進行。 That is, in the epoxy resin of the formula (2), n = 0 (4 functional groups) When the proportion of the fraction is increased, the ethylene unit is closest to the phenyl epoxidone unit by 1:4. On the other hand, when a polyvalent hydroxy compound having a higher ratio of n=1 (7-functional) and n=2 (10-functional) components of a higher functional component is used, the ratio is 2:7 and 3:10, and the ratio is The density of the joint is denser, and the hardened material excellent in heat stability can be obtained by relatively small units of the glycidyl ether. Moreover, it is considered that when a polyfunctional component is added, a hardened substance is used in the reaction with the hardener. The crosslink density is increased, and it can also be a cured product having more excellent thermal stability. However, when the component of n=5 or more is added, since the molecular weight is increased, fluidity or moldability tends to be deteriorated. For this reason, the number of n-ranges 0 to 10 includes n=0, and the average (number average) of n is preferably in the range of 0.1 to 4. Since n is substantially inherited from n of the polyvalent hydroxy compound used as a raw material, the adjustment of n is carried out by adjusting n of the polyvalent hydroxy compound.

本發明之環氧樹脂可藉由上述多元羥基樹脂 與表氯醇反應而製造。該反應可與通常之環氧化反應同樣地進行。列舉為例如,將多元羥基樹脂溶解於過量之表氯醇中之後,在氫氧化鈉、氫氧化鉀等之鹼金屬氫氧化物之存在下,在50~150℃、較好在60~120℃反應1~10小時之方法。此時,鹼金屬氫氧化物之使用量相對於多元羥基化合物中之羥基1莫耳,為0.8~1.2莫耳,較好為0.9~1.0莫耳。另外,表氯醇相對於多元羥基樹脂中之羥基雖為過量使用,但通常相對於多元羥基化合物中之羥基1莫耳為1.5~15莫耳,較好為2~8莫耳。反應結束後,可餾除過量表氯醇,將殘留物溶解於甲苯、甲基異丁基酮等溶劑中,經過濾、水洗去除無機鹽,接著餾除溶劑,而獲得以通式(2)表示之環氧樹脂。但,環氧化反應時環氧丙基與未反應之酚性羥基之反應亦會進行,亦生成以環氧丙基連結之多聚物,故需要將反應條件調整在上述範圍。 與4官能之環氧化合物之多聚物意義上為相同,但因結合部位不同故而耐熱性有較大差異。 The epoxy resin of the present invention can be obtained by the above polyhydric hydroxy resin Manufactured by reacting with epichlorohydrin. This reaction can be carried out in the same manner as in the usual epoxidation reaction. For example, after dissolving the polyhydric hydroxy resin in an excess of epichlorohydrin, in the presence of an alkali metal hydroxide such as sodium hydroxide or potassium hydroxide, at 50 to 150 ° C, preferably 60 to 120 ° C. The method of reacting for 1 to 10 hours. At this time, the amount of the alkali metal hydroxide to be used is 0.8 to 1.2 moles, preferably 0.9 to 1.0 moles, per mole of the hydroxyl group in the polyvalent hydroxy compound. Further, although epichlorohydrin is used in excess with respect to the hydroxyl group in the polyhydric hydroxy resin, it is usually 1.5 to 15 moles, preferably 2 to 8 moles per mole of the hydroxyl group in the polyvalent hydroxy compound. After the completion of the reaction, the excess epichlorohydrin can be distilled off, and the residue is dissolved in a solvent such as toluene or methyl isobutyl ketone, and the inorganic salt is removed by filtration and washing with water, followed by distilling off the solvent to obtain the formula (2). Indicates the epoxy resin. However, the reaction of the epoxidized propyl group with the unreacted phenolic hydroxyl group also proceeds during the epoxidation reaction, and a polymer which is linked by a propylene group is also formed. Therefore, it is necessary to adjust the reaction conditions to the above range. The polymer of the tetrafunctional epoxy compound is the same, but the heat resistance is largely different depending on the binding site.

另外,該環氧樹脂之黏度及軟化點可藉由改 變合成環氧樹脂原料的多元羥基樹脂時之酚化合物與乙二醛之莫耳比而可容易地調整,但就無機填料高填充化之觀點而言,其黏度於150℃之熔融黏度較好為3.0Pa.s以下,更好為1.0Pa.s以下,又更好為0.5Pa.s以下。另外,其軟化點較好為130℃以下。 In addition, the viscosity and softening point of the epoxy resin can be modified The molar ratio of the phenolic compound to the glyoxal of the polyhydroxy resin in the synthesis of the epoxy resin can be easily adjusted, but the viscosity of the inorganic filler is better at 150 ° C from the viewpoint of high filling of the inorganic filler. It is 3.0Pa. s below, better for 1.0Pa. Below s, it is better to 0.5Pa. s below. Further, the softening point thereof is preferably 130 ° C or lower.

接著,針對本發明之環氧樹脂組成物加以說 明。本發明之環氧樹脂組成物包含上述本發明之環氧樹脂、硬化劑、硬化觸媒及無機填充劑。此處,本發明之環氧樹脂係以通式(2)表示之環氧樹脂、或以通式(1)表示之多元羥基化合物與表氯醇反應獲得之環氧樹脂。 Next, the epoxy resin composition of the present invention is said Bright. The epoxy resin composition of the present invention comprises the above-mentioned epoxy resin, hardener, hardening catalyst and inorganic filler of the present invention. Here, the epoxy resin of the present invention is an epoxy resin obtained by reacting an epoxy resin represented by the formula (2) or a polyvalent hydroxy compound represented by the formula (1) with epichlorohydrin.

該環氧樹脂組成物中調配之硬化劑係使用酚 系硬化劑。在要求半導體密封材等之高電氣絕緣性之領域中,較好使用多元酚類作為硬化劑。以下列出硬化劑之具體例。 The hardener used in the epoxy resin composition is phenol A hardener. In the field of requiring high electrical insulation properties of semiconductor sealing materials and the like, polyphenols are preferably used as the curing agent. Specific examples of the hardener are listed below.

多元酚類有例如以雙酚A、雙酚F、雙酚S、 茀雙酚、對苯二酚、間苯二酚、兒茶酚、聯酚類、萘二酚類等2元之酚類,以及參-(4-羥基苯基)甲烷、1,1,2,2-肆(4-羥基苯基)乙烷、酚酚醛清漆、鄰-甲酚酚醛清漆、萘酚酚醛清漆、二環戊二烯型酚樹脂、酚芳烷基樹脂等為代表之3元以上之酚類等。進而,有酚類、萘酚類、或雙酚A、雙酚F、雙酚S、茀雙酚、4,4’-聯酚、2,2’-聯酚、對苯二酚、間苯二酚、兒茶酚、萘二酚類等2元酚類與甲醛、乙醛、苯甲醛、對-羥基苯甲醛、對-二甲苯二醇、對-二甲苯二醇二甲醚、二乙烯基苯、二異丙烯基苯、二甲氧 基甲基聯苯類、二乙烯基聯苯、二異丙烯基聯苯類等之交聯劑反應而合成之多元酚性化合物,由酚類與雙氯甲基聯苯等所得之聯苯芳烷基型酚樹脂等。進而,列舉為由萘酚類與二氯化對二甲苯等合成之萘酚芳烷基樹脂類、以通式(1)表示之多元羥基化合物等。 The polyphenols are, for example, bisphenol A, bisphenol F, bisphenol S, Bisphenol, hydroquinone, resorcinol, catechol, biphenols, naphthalenediols, etc. 2 phenols, and ginseng-(4-hydroxyphenyl)methane, 1,1,2 , 2-anthracene (4-hydroxyphenyl)ethane, phenol novolac, o-cresol novolac, naphthol novolac, dicyclopentadiene phenol resin, phenol aralkyl resin, etc. The above phenols and the like. Further, there are phenols, naphthols, or bisphenol A, bisphenol F, bisphenol S, bismuth bisphenol, 4,4'-biphenol, 2,2'-biphenol, hydroquinone, and isophthalic acid. Diphenols such as diphenol, catechol, naphthalenediol and formaldehyde, acetaldehyde, benzaldehyde, p-hydroxybenzaldehyde, p-xylene glycol, p-xylene glycol dimethyl ether, diethylene Benzobenzene, diisopropenylbenzene, dimethoxy A polyphenolic compound synthesized by a crosslinking reaction of a methylated biphenyl, a divinylbiphenyl or a diisopropenylbiphenyl, and a biphenyl aryl obtained from a phenol or a bischloromethylbiphenyl. An alkyl type phenol resin or the like. Further, examples thereof include naphthol aralkyl resins synthesized from naphthols and p-xylene dichloride, and polyvalent hydroxy compounds represented by the formula (1).

硬化劑之調配量係考慮環氧樹脂中之環氧基 與多元酚類之羥基之當量均衡而調配。環氧樹脂及硬化劑之當量比通常為0.2至5.0之範圍,較好為0.5至2.0之範圍,更好為0.8~1.5之範圍。大於或小於其時,均會使環氧樹脂組成物之硬化性降低,並且降低硬化物之耐熱性、力學強度等。 The amount of hardener is determined by considering the epoxy group in the epoxy resin. It is formulated in an equilibrium with the equivalent of the hydroxyl group of the polyhydric phenol. The equivalent ratio of the epoxy resin and the hardener is usually in the range of 0.2 to 5.0, preferably in the range of 0.5 to 2.0, more preferably in the range of 0.8 to 1.5. When it is larger or smaller, the hardenability of the epoxy resin composition is lowered, and the heat resistance, mechanical strength, and the like of the cured product are lowered.

又,該環氧樹脂組成物中,亦可調配芳香族 羥基化合物以外之他種硬化劑作為硬化劑成分。該情況之環氧樹脂有例如二胺二醯胺、酸酐類、芳香族及脂肪族胺類等。該等樹脂組成物中可使用該等硬化劑之1種或混合2種以上使用。然而,酚系硬化劑以外之硬化劑之使用量較好為全部硬化劑之50wt%以下。 Moreover, the epoxy resin composition may also be formulated with aromatic Other hardeners other than the hydroxy compound are used as the hardener component. The epoxy resin in this case is, for example, a diamine diamine, an acid anhydride, an aromatic or an aliphatic amine. One type of these hardening agents or a mixture of two or more types may be used for the resin composition. However, the amount of the curing agent other than the phenolic curing agent is preferably 50% by weight or less based on the total amount of the curing agent.

又,該環氧樹脂組成物中,亦可調配以通式 (2)表示之環氧樹脂以外之他種環氧樹脂作為環氧樹脂成分。作為該情況之環氧樹脂,於分子中具有2個以上環氧基之一般環氧樹脂全部可使用。例如列舉為由雙酚A、雙酚F、雙酚S、茀雙酚、4,4’-聯酚、3,3’,5,5’-四甲基-4,4’-二羥基聯苯、間苯二酚、萘二酚類等2元酚類之環氧化物,參-(4-羥基苯基)甲烷、1,1,2,2-肆(4-羥基苯基)乙烷、 酚酚醛清漆、鄰-甲酚酚醛清漆等3元以上酚類之環氧化物,由二環戊二烯與酚類所得之共縮合樹脂之環氧化物,由甲酚類與甲醛及烷氧基取代之萘類所得之共縮合樹脂環氧化物,由酚類與二氯化對二甲苯等所得之酚芳烷基樹脂之環氧化物,由酚類與雙氯甲基聯苯等所得之聯苯芳烷基型酚樹脂之環氧化物,由萘酚類與二氯化對二甲苯等所合成之萘酚芳烷基樹脂類之環氧化物等。該等環氧樹脂可使用1種或混合2種以上使用。而且,以本發明之環氧樹脂作為必要成分之組成物時,以通式(2)表示之環氧樹脂之調配量在環氧樹脂整體中宜為5~100wt%,較好為60~100wt%之範圍。 Moreover, the epoxy resin composition can also be formulated with a general formula (2) Other epoxy resins other than the epoxy resin shown as the epoxy resin component. As the epoxy resin in this case, all of the general epoxy resins having two or more epoxy groups in the molecule can be used. For example, it is exemplified by bisphenol A, bisphenol F, bisphenol S, bisphenol, 4,4'-biphenol, 3,3',5,5'-tetramethyl-4,4'-dihydroxyl Epoxides of 2-membered phenols such as benzene, resorcinol and naphthalenediol, ginseng-(4-hydroxyphenyl)methane, 1,1,2,2-indole (4-hydroxyphenyl)ethane , An epoxide of a phenolic phenolic varnish, an o-cresol novolac, and the like, a epoxide of a diol of three or more phenols, an epoxide of a co-condensation resin obtained from dicyclopentadiene and a phenol, and a cresol, a formaldehyde, and an alkoxy group. a condensed resin epoxide obtained by substituting a naphthalene, an epoxide of a phenol aralkyl resin obtained from a phenol and a p-xylene dichloride, and a phenol and a bischloromethylbiphenyl. An epoxide of a phenylaralkyl type phenol resin, an epoxide of a naphthol aralkyl resin synthesized from naphthols and p-xylene dichloride, and the like. These epoxy resins may be used alone or in combination of two or more. Further, when the epoxy resin of the present invention is used as a constituent of the essential component, the amount of the epoxy resin represented by the formula (2) is preferably from 5 to 100% by weight, preferably from 60 to 100% by weight in the entire epoxy resin. The range of %.

無機填充劑列舉為球狀或破碎狀之熔融二氧 化矽、結晶二氧化矽等二氧化矽粉末、氧化鋁粉末、玻璃粉末、或雲母、滑石、碳酸鈣、氧化鋁、水合氧化鋁、氮化硼、氮化鋁、氮化矽、碳化矽、氮化鈦、氧化鋅、碳化鎢、氧化鎂等。使用於半導體密封材時之較佳調配量為70重量%以上,更好為80重量%以上。 Inorganic fillers are listed as spherical or broken molten dioxins Cerium oxide powder such as bismuth oxide or cerium oxide, alumina powder, glass powder, or mica, talc, calcium carbonate, alumina, hydrated alumina, boron nitride, aluminum nitride, tantalum nitride, tantalum carbide, Titanium nitride, zinc oxide, tungsten carbide, magnesium oxide, and the like. A preferred blending amount for use in the semiconductor sealing material is 70% by weight or more, more preferably 80% by weight or more.

作為硬化觸媒,基於促進硬化並且提高成形 時之流動性之目的,較好使用環氧樹脂組成物中在高溫區域具有活性點之硬化觸媒(高溫活性觸媒)。 As a hardening catalyst, it promotes hardening and improves forming For the purpose of fluidity at the time, it is preferred to use a hardening catalyst (high temperature active catalyst) having an active point in a high temperature region in the epoxy resin composition.

硬化觸媒之含量相對於環氧樹脂100重量份 為0.2~5重量份之範圍。較好為0.5~3重量份,更好為0.5~2.5重量份。小於該值時,硬化性降低,且相反地比其大時,無法充分展現成形時之流動性提高效果。 The content of the hardening catalyst is 100 parts by weight relative to the epoxy resin It is in the range of 0.2 to 5 parts by weight. It is preferably from 0.5 to 3 parts by weight, more preferably from 0.5 to 2.5 parts by weight. When the value is less than this value, the curability is lowered, and conversely, when it is larger than this, the fluidity improving effect at the time of molding cannot be sufficiently exhibited.

使用高溫活性觸媒之環氧樹脂組成物之DSC 發熱峰溫度為150℃以上,較好為155℃以上,更好為165℃以上。發熱峰溫度低於150℃時成形時進行硬化反應而無法充分展現流動性提高效果。該DSC發熱峰溫度係以升溫速度10℃/分鐘之條件,DSC測定調配有作為硬化觸媒之高溫活性觸媒之環氧樹脂組成物時顯示最大發熱峰之溫度。 DSC of epoxy resin composition using high temperature active catalyst The exothermic peak temperature is 150 ° C or higher, preferably 155 ° C or higher, more preferably 165 ° C or higher. When the exothermic temperature is lower than 150 ° C, the curing reaction proceeds at the time of molding, and the fluidity improving effect cannot be sufficiently exhibited. The DSC exothermic peak temperature was measured at a temperature rising rate of 10 ° C /min, and the temperature at which the maximum exothermic peak was exhibited when the epoxy resin composition as a high-temperature active catalyst of the curing catalyst was prepared by DSC measurement.

至於硬化觸媒或高溫活性觸媒若舉例,則列 舉為咪唑類、有機膦類、胺類等。咪唑類列舉為2-苯基-4,5-二羥基甲基咪唑、2-苯基-4-甲基-5-羥基甲基咪唑、2-十七烷基咪唑、2,4-二胺基-6-[2’-二甲基咪唑基-(1’)]-乙基-s-三嗪、2,4-二胺基-6-[2’-乙基-4’-甲基咪唑基-(1’)]-乙基-s-三嗪、2,4-二胺基-6-[2’-十一烷基咪唑基-(1’)]-乙基-s-三嗪等,有機膦類列舉為參-(2,6-二甲氧基苯基)膦、三-對-甲苯基膦、參(對-氯苯基)膦、參(對-甲氧基苯基)膦等,胺類列舉為1,8-二氮雜雙環(5.4.0)十一碳烯-7之酚酚醛清漆鹽等。添加量通常相對於環氧樹脂100重量份為0.2~5重量份之範圍。 As for the hardening catalyst or high temperature active catalyst, for example, Examples are imidazoles, organophosphines, amines, and the like. The imidazoles are exemplified by 2-phenyl-4,5-dihydroxymethylimidazole, 2-phenyl-4-methyl-5-hydroxymethylimidazole, 2-heptadecylimidazole, 2,4-diamine. -6-[2'-dimethylimidazolyl-(1')]-ethyl-s-triazine, 2,4-diamino-6-[2'-ethyl-4'-methyl Imidazolyl-(1')]-ethyl-s-triazine, 2,4-diamino-6-[2'-undecylimidazolyl-(1')]-ethyl-s-three Oxazine, etc., organophosphines are exemplified by gins-(2,6-dimethoxyphenyl)phosphine, tri-p-tolylphosphine, ginseng (p-chlorophenyl)phosphine, and para-p-methoxybenzene. The phosphines and the like are exemplified by 1,8-diazabicyclo (5.4.0) undecenene-7 phenol novolac salt and the like. The amount of addition is usually in the range of 0.2 to 5 parts by weight based on 100 parts by weight of the epoxy resin.

本發明中,藉由使用具有特定之活性溫度區 域之高溫活性觸媒作為硬化觸媒,可抑制流動性之降低,再者關於硬化條件,發現尤其在使用本發明之環氧樹脂時,在特殊高溫之硬化條件對於玻璃轉移溫度造成較大影響。 In the present invention, by using a specific active temperature region The high-temperature active catalyst of the domain acts as a hardening catalyst to suppress the decrease of fluidity. Further, regarding the hardening conditions, it is found that the hardening conditions at special high temperatures have a great influence on the glass transition temperature especially when the epoxy resin of the present invention is used. .

本發明之樹脂組成物中可視需要使用巴西棕 櫚蠟(carnauba wax)、OP蠟等脫模劑,4-胺基丙基乙氧基矽烷、γ-環氧丙氧基丙基三甲氧基矽烷等偶合劑,碳黑等著色劑,三氧化銻等難燃劑、硬脂酸鈣等滑劑等。 The Brazilian resin brown body can be used as needed in the resin composition of the present invention. Release agent such as carnauba wax, OP wax, coupling agent such as 4-aminopropyl ethoxy decane, γ-glycidoxypropyltrimethoxy decane, coloring agent such as carbon black, and trioxide A flame retardant such as ruthenium or a slip agent such as calcium stearate.

本發明之環氧樹脂組成物中亦可適當調配聚 酯、聚醯胺、聚醯亞胺、聚醚、聚胺基甲酸酯、石油樹脂、茚樹脂、茚.香豆滿樹脂、苯氧樹脂等之寡聚物或高分子化合物作為其他改質劑。添加量通常相對於環氧樹脂100重量份為2~30重量份之範圍。 The epoxy resin composition of the present invention can also be appropriately formulated and polymerized. Ester, polyamide, polyimine, polyether, polyurethane, petroleum resin, enamel resin, hydrazine. An oligo or a polymer compound of a coumarin-filled resin or a phenoxy resin is used as another modifier. The amount of addition is usually in the range of 2 to 30 parts by weight based on 100 parts by weight of the epoxy resin.

另外,本發明之環氧樹脂組成物中可調配顏 料、難燃劑、搖變性賦予劑、偶合劑、流動性提升劑、抗氧化劑等添加劑。 In addition, the epoxy resin composition of the invention can be adjusted Additives such as materials, flame retardants, shake imparting agents, coupling agents, fluidity enhancers, and antioxidants.

至於顏料,有有機系或無機系之體質顏料、 鱗片狀顏料等。搖變性賦予劑可列舉為矽系、蓖麻油系、脂肪族醯胺蠟、氧化聚乙烯蠟、有機膨潤土系等。 As for the pigment, there are organic or inorganic body pigments, Flaky pigments, etc. Examples of the shake imparting agent include an anthraquinone-based, a castor oil-based, an aliphatic guanamine wax, an oxidized polyethylene wax, and an organic bentonite-based.

本發明之環氧樹脂組成物可以有機溶劑溶解 作成漆料狀態後,含浸於玻璃布、芳醯胺不織布、液晶聚合物等之聚酯不織布等之纖維狀物中之後進行溶劑去除,成為預浸體。另外,可視情況塗佈於銅箔、不鏽鋼箔、聚醯亞胺薄膜、聚酯薄膜等之薄片狀物上成為層合物。 The epoxy resin composition of the present invention can be dissolved in an organic solvent After being in a paint state, it is impregnated into a fibrous material such as a glass cloth, an linoleamide nonwoven fabric, or a liquid crystal polymer such as a polyester nonwoven fabric, and then removed by a solvent to obtain a prepreg. Further, it may be applied to a sheet of a copper foil, a stainless steel foil, a polyimide film, a polyester film or the like as a laminate as the case may be.

本發明之環氧樹脂組成物之調製方法若為可 均勻地分散混合各種原材料則可使用任何方法,作為一般方法列舉為以混練機等充分混合特定調配量之原材料後,以混合輥、擠出機等熔融混練,經冷卻、粉碎之方法。 The preparation method of the epoxy resin composition of the present invention is Any method can be used to uniformly disperse and mix the various raw materials. As a general method, a material which is sufficiently mixed with a specific blending amount by a kneading machine or the like is melt-kneaded by a mixing roll or an extruder, and is cooled and pulverized.

本發明之環氧樹脂組成物及其硬化物尤其適 於作為半導體裝置之密封用。 The epoxy resin composition of the present invention and the hardened material thereof are particularly suitable Used as a seal for semiconductor devices.

本發明之硬化物可藉由使上述環氧樹脂組成 物熱硬化而得。為了使用本發明之環氧樹脂組成物獲得硬化物,可應用例如轉模成形、加壓成形、注模成形、射出成形、擠出成形等方法,但就量產性之觀點而言,以轉模成形較佳。 The cured product of the present invention can be composed of the above epoxy resin The material is hardened by heat. In order to obtain a cured product using the epoxy resin composition of the present invention, methods such as transfer molding, press molding, injection molding, injection molding, extrusion molding, and the like can be applied, but in terms of mass productivity, Mold forming is preferred.

本發明之環氧樹脂組成物之硬化方法係在100 ℃~200℃,較好在120℃~190℃,更好在150~180℃成形後,在200℃~300℃,較好在220℃~280℃,更好在230~270℃下後硬化而製造,可獲得高耐熱性、高溫長期熱分解安定性及高流動性等方面優異之硬化物。 The hardening method of the epoxy resin composition of the present invention is 100 °C~200°C, preferably 120°C~190°C, better after forming at 150~180°C, after 200°C~300°C, preferably 220°C~280°C, better after 230~270°C By manufacturing, it is possible to obtain a cured product excellent in heat resistance, high-temperature long-term thermal decomposition stability, and high fluidity.

成形時間較好為1~60分鐘,更好為1分鐘至10分鐘。成形時間變長時生產性變差,過短時難以脫模。後硬化時間較好為10分鐘~10小時,更好為30分鐘~8小時,最好為2小時~6小時。後硬化時間短時硬化無法充分進行,無法獲得耐熱性或機械特性等充分之特性。且,超過10小時時生產性降低。 The forming time is preferably from 1 to 60 minutes, more preferably from 1 minute to 10 minutes. When the forming time is long, the productivity is deteriorated, and when it is too short, it is difficult to demold. The post-hardening time is preferably from 10 minutes to 10 hours, more preferably from 30 minutes to 8 hours, and most preferably from 2 hours to 6 hours. When the post-hardening time is short, the hardening cannot be sufficiently performed, and sufficient characteristics such as heat resistance and mechanical properties cannot be obtained. Moreover, productivity is lowered over 10 hours.

本發明之環氧樹脂組成物即使在一般環氧樹 脂組成物無法反應之高後硬化溫度區域中亦可進行硬化反應,可獲得具有非常高之耐熱性、耐熱分解性、機械物性等之硬化物。 The epoxy resin composition of the present invention is even in general epoxy trees When the fat composition is not able to react, the hardening reaction can be carried out in the hardening temperature region, and a cured product having extremely high heat resistance, thermal decomposition resistance, mechanical properties, and the like can be obtained.

[實施例] [Examples]

以下基於合成例、實施例及比較例具體說明 本發明。 The following is specifically described based on synthesis examples, examples, and comparative examples. this invention.

合成例1 Synthesis Example 1

於5L之4頸燒瓶中饋入苯酚3500g(37.2莫耳)及作為酸觸媒之對-甲苯磺酸2.36g,升溫至50℃。接著,邊在50℃攪拌邊於30分鐘滴加40%乙二醛水溶液360g,於滴加結束後於50℃反應30分鐘,於100℃反應2小時。接著,減壓下在100℃進行脫水後,在100℃反應4小時。反應結束後,餾除苯酚,獲得酚樹脂711g。所得樹脂之羥基當量為119.4g/eq.。且,由GPC測定結果,n=0之成分:71.5%,n=1以上之成分:13.2%。 3,500 g (37.2 mol) of phenol and 2.36 g of p-toluenesulfonic acid as an acid catalyst were fed into a 5 L four-necked flask, and the temperature was raised to 50 °C. Next, 360 g of a 40% aqueous solution of glyoxal was added dropwise thereto over 30 minutes while stirring at 50 ° C, and after the completion of the dropwise addition, the mixture was reacted at 50 ° C for 30 minutes, and reacted at 100 ° C for 2 hours. Subsequently, the mixture was dehydrated at 100 ° C under reduced pressure, and then reacted at 100 ° C for 4 hours. After completion of the reaction, phenol was distilled off to obtain 711 g of a phenol resin. The hydroxyl equivalent of the obtained resin was 119.4 g/eq. Further, as a result of GPC measurement, the component of n=0: 71.5%, and the component of n=1 or more: 13.2%.

合成例2 Synthesis Example 2

於5L之4頸燒瓶中饋入合成例1中獲得之酚樹脂500g、二乙二醇二甲醚377g、表氯醇2511g且升溫至60℃。接著,在2小時內滴加49%氫氧化鉀水溶液48.2g進行預反應後,減壓下於63℃,以3.5小時內滴加49%氫氧化鈉水溶液298.9g,且以分離槽分離該滴加中回流餾出之水與表氯醇且使表氯醇回到反應容器中,將水排出於系統外進行反應。反應結束後,以過濾去除生成之鹽,再經水洗後餾除表氯醇,獲得環氧樹脂660g(環氧樹脂A)。所得樹脂之環氧當量為182.0g/eq.,於150℃之熔融黏度為0.35Pa.s。 500 g of the phenol resin obtained in Synthesis Example 1, 377 g of diethylene glycol dimethyl ether, and 2511 g of epichlorohydrin were fed into a 5 L four-necked flask, and the temperature was raised to 60 °C. Next, 48.2 g of a 49% potassium hydroxide aqueous solution was added dropwise thereto over 2 hours to carry out a preliminary reaction, and then 298.9 g of a 49% aqueous sodium hydroxide solution was added dropwise thereto at 63 ° C for 3.5 hours under reduced pressure, and the droplet was separated by a separation tank. The water distilled off under reflux is added to epichlorohydrin and the epichlorohydrin is returned to the reaction vessel, and the water is discharged outside the system for reaction. After completion of the reaction, the resulting salt was removed by filtration, and then washed with water, and then epichlorohydrin was distilled off to obtain 660 g of epoxy resin (epoxy resin A). The epoxy equivalent of the obtained resin was 182.0 g/eq., and the melt viscosity at 150 ° C was 0.35 Pa. s.

合成例3 Synthesis Example 3

於3L之4頸燒瓶中饋入苯酚1000g及40重量%乙二醛水溶液232g及丙酮125g,在2小時內滴加95重量%之硫酸187.5g。隨後,在40℃進行反應12小時,反應結束後,冷卻至15℃進行中和。接著,添加丙酮632g,過濾析出物。接著,以丙酮與水之混合液洗淨,饋入甲醇1400g,加熱回流約1小時溶解後,經熱時過濾去除中和鹽。另一方面,所得甲醇溶液在攪拌下添加564g水後,經減壓蒸餾餾除甲醇。隨後,在15℃攪拌隔夜後,過濾分離,在約130℃減壓乾燥,獲得白色結晶之肆酚乙烷227g。所得樹脂之羥基當量為103.8g/eq.。且,由GPC測定結果,為n=0成分:100%。 Into a 3 L four-necked flask, 1000 g of phenol, 232 g of a 40% by weight aqueous solution of glyoxal, and 125 g of acetone were fed, and 187.5 g of 95% by weight of sulfuric acid was added dropwise over 2 hours. Subsequently, the reaction was carried out at 40 ° C for 12 hours, and after completion of the reaction, it was cooled to 15 ° C for neutralization. Next, 632 g of acetone was added, and the precipitate was filtered. Subsequently, the mixture was washed with a mixture of acetone and water, and 1400 g of methanol was fed thereto, and the mixture was heated and refluxed for about 1 hour to dissolve, and then the neutralized salt was removed by filtration while being heated. On the other hand, after the obtained methanol solution was added with 564 g of water under stirring, methanol was distilled off under reduced pressure. Subsequently, after stirring overnight at 15 ° C, it was separated by filtration, and dried under reduced pressure at about 130 ° C to obtain 227 g of a white crystal of phenol. The hydroxyl equivalent of the obtained resin was 103.8 g/eq. Further, as a result of GPC measurement, it was n=0 component: 100%.

合成例4 Synthesis Example 4

於5L之4頸燒瓶中饋入合成例3中獲得之酚樹脂500g、二乙二醇二甲醚434g、表氯醇2896g且升溫至60℃。接著,在2小時內滴加49%氫氧化鉀水溶液55.5g進行預反應後,減壓下於63℃,在3.5小時滴加49%氫氧化鈉水溶液344.6g,且以分離槽分離該滴加中回流餾出之水與表氯醇且使表氯醇回到反應容器中,將水排出於系統外進行反應。反應結束後,藉過濾去除生成之鹽,再經水洗後餾除表氯醇,獲得環氧樹脂693g(環氧樹脂B)。所得樹脂之環氧當量為173.0g/eq.,藉由DSC確認為具有181℃之熔點之結晶性樹脂。 500 g of the phenol resin obtained in Synthesis Example 3, 434 g of diethylene glycol dimethyl ether, and 2896 g of epichlorohydrin were fed into a 5 L four-necked flask, and the temperature was raised to 60 °C. Next, 55.5 g of a 49% potassium hydroxide aqueous solution was added dropwise for 2 hours to carry out a preliminary reaction, and then 344.6 g of a 49% aqueous sodium hydroxide solution was added dropwise at 63 ° C for 3.5 hours under reduced pressure, and the dropwise addition was separated by a separation tank. The distilled water is refluxed with epichlorohydrin and the epichlorohydrin is returned to the reaction vessel, and the water is discharged outside the system for reaction. After completion of the reaction, the salt formed was removed by filtration, and then washed with water to distill off epichlorohydrin to obtain 693 g of an epoxy resin (epoxy resin B). The obtained resin had an epoxy equivalent of 173.0 g/eq., which was confirmed to be a crystalline resin having a melting point of 181 ° C by DSC.

合成例5 Synthesis Example 5

於5L之4頸燒瓶中饋入苯酚3500g(37.2莫耳)及作為酸觸媒之對-甲苯磺酸1.77g,升溫至50℃。接著,邊在50℃攪拌邊於30分鐘內滴加40%乙二醛水溶液270g,於滴加結束後在50℃反應1小時,在60℃反應2.5小時。接著,減壓下於60℃進行脫水後,在60℃反應8.5小時。反應結束後,餾除苯酚,獲得酚樹脂534g。所得樹脂之羥基當量為112.0g/eq.。且,由GPC測定結果,n=0之成分:79.3%,n=1以上之成分:8.6%。 3,500 g (37.2 mol) of phenol and 1.77 g of p-toluenesulfonic acid as an acid catalyst were fed into a 5 L four-necked flask, and the temperature was raised to 50 °C. Next, 270 g of a 40% aqueous solution of glyoxal was added dropwise thereto over 30 minutes while stirring at 50 ° C, and after the completion of the dropwise addition, the reaction was carried out at 50 ° C for 1 hour, and at 60 ° C for 2.5 hours. Subsequently, the mixture was dehydrated at 60 ° C under reduced pressure, and then reacted at 60 ° C for 8.5 hours. After completion of the reaction, phenol was distilled off to obtain 534 g of a phenol resin. The hydroxyl equivalent of the obtained resin was 112.0 g/eq. Further, as a result of GPC measurement, the component of n = 0: 79.3%, and the component of n = 1 or more: 8.6%.

合成例6 Synthesis Example 6

於5L之4頸燒瓶中饋入合成例5中獲得之酚樹脂500g、二乙二醇二甲醚403g、表氯醇2684g且升溫至60℃。接著,在2小時內滴加49%氫氧化鉀水溶液51.5g進行預反應後,減壓下於63℃,以3.5小時內滴加49%氫氧化鈉水溶液315.3g,以分離槽分離該滴加中回流餾出之水與表氯醇,使表氯醇回到反應容器中,且將水排出於系統外進行反應。反應結束後,藉過濾去除生成之鹽,再經水洗餾除表氯醇,獲得環氧樹脂675g(環氧樹脂D)。所得樹脂之環氧當量為179.5g/eq.。於150℃之熔融黏度為0.28Pa.s。 500 g of the phenol resin obtained in Synthesis Example 5, 403 g of diethylene glycol dimethyl ether, and 2684 g of epichlorohydrin were fed into a 5 L four-necked flask, and the temperature was raised to 60 °C. Next, 51.5 g of a 49% potassium hydroxide aqueous solution was added dropwise thereto over 2 hours to carry out a preliminary reaction, and then 315.3 g of a 49% aqueous sodium hydroxide solution was added dropwise thereto at 63 ° C for 3.5 hours under reduced pressure to separate the dropwise addition in a separation tank. The distilled water and epichlorohydrin are refluxed to return epichlorohydrin to the reaction vessel, and the water is discharged outside the system for reaction. After completion of the reaction, the salt formed was removed by filtration, and epichlorohydrin was distilled off by water to obtain 675 g of epoxy resin (epoxy resin D). The epoxy equivalent of the obtained resin was 179.5 g/eq. The melt viscosity at 150 ° C is 0.28 Pa. s.

合成例7 Synthesis Example 7

於5L之4頸燒瓶中饋入苯酚300g(3.2莫耳)及作為酸觸媒之對-甲苯磺酸1.01g,升溫至50℃。接著,邊在50℃攪拌邊於30分鐘內滴加40%乙二醛水溶液154g,於滴加結束後在50℃反應30分鐘,在100℃反應2小時。接著,於減壓下在100℃進行脫水後,在100℃反應4小時。反應結束後,餾除苯酚,獲得酚樹脂226g。所得樹脂之羥基當量為130.6g/eq.。且,由GPC測定結果,n=0之成分:29.9%,n=1以上之成分:55.3%。 Into a 5 L four-necked flask, 300 g (3.2 mol) of phenol and 1.01 g of p-toluenesulfonic acid as an acid catalyst were fed, and the temperature was raised to 50 °C. Next, 154 g of a 40% aqueous solution of glyoxal was added dropwise thereto over 30 minutes while stirring at 50 ° C, and after the completion of the dropwise addition, the reaction was carried out at 50 ° C for 30 minutes, and at 100 ° C for 2 hours. Subsequently, the mixture was dehydrated at 100 ° C under reduced pressure, and then reacted at 100 ° C for 4 hours. After completion of the reaction, phenol was distilled off to obtain 226 g of a phenol resin. The hydroxyl equivalent of the obtained resin was 130.6 g/eq. Further, as a result of GPC measurement, the component of n = 0: 29.9%, and the component of n = 1 or more: 55.3%.

合成例8 Synthesis Example 8

於5L之4頸燒瓶中饋入合成例7中獲得之酚樹脂125g、二乙二醇二甲醚86g、表氯醇575g且升溫至60℃。接著,在2小時內滴加49%氫氧化鉀水溶液11.0g進行預反應後,減壓下於63℃,以3.5小時內滴加49%氫氧化鈉水溶液67.5g,以分離槽分離該滴加中回流餾出之水與表氯醇且使表氯醇回到反應容器中,將水排出於系統外進行反應。反應結束後,藉過濾去除生成之鹽,再經水洗後餾除表氯醇,獲得環氧樹脂70g(環氧樹脂E)。所得樹脂之環氧當量為209.6g/eq.。於150℃之熔融黏度為3.08Pa.s。 125 g of the phenol resin obtained in Synthesis Example 7, 86 g of diethylene glycol dimethyl ether, and 575 g of epichlorohydrin were fed into a 5 L four-necked flask, and the temperature was raised to 60 °C. Next, 11.0 g of a 49% potassium hydroxide aqueous solution was added dropwise thereto over 2 hours to carry out a preliminary reaction, and then 67.5 g of a 49% aqueous sodium hydroxide solution was added dropwise thereto at 63 ° C for 3.5 hours under reduced pressure, and the dropwise addition was separated by a separation tank. The distilled water is refluxed with epichlorohydrin and the epichlorohydrin is returned to the reaction vessel, and the water is discharged outside the system for reaction. After completion of the reaction, the resulting salt was removed by filtration, and after washing with water, epichlorohydrin was distilled off to obtain 70 g of epoxy resin (epoxy resin E). The epoxy equivalent of the obtained resin was 209.6 g/eq. The melt viscosity at 150 ° C is 3.08 Pa. s.

合成例1、3、5、7中獲得之酚樹脂之GPC圖譜示於圖1、3、5、7,合成例2、4、6、8中獲得之環氧樹脂之GPC圖譜示於圖2、4、6、8。 The GPC patterns of the phenol resins obtained in Synthesis Examples 1, 3, 5, and 7 are shown in Figs. 1, 3, 5, and 7, and the GPC patterns of the epoxy resins obtained in Synthesis Examples 2, 4, 6, and 8 are shown in Fig. 2. , 4, 6, and 8.

實施例1 Example 1

使用合成例2中獲得之環氧樹脂A 100g作為環氧樹脂成分、酚酚醛清漆(PSM-4324(群榮化學工業股份有限公司製),OH當量105、軟化點:100℃)57.5g作為硬化劑成分。另外,使用硬化促進劑A;2-甲基咪唑(東京化成股份有限公司製)0.7g,經混練獲得環氧樹脂組成物。使用該環氧樹脂組成物,以成形溫度175℃、3分鐘、後硬化溫度250℃、5小時之條件(成形條件A)獲得硬化物試驗片後,測定5%重量減少溫度。結果示於表1。 100 g of the epoxy resin A obtained in Synthesis Example 2 was used as an epoxy resin component, and a phenol novolak (PSM-4324 (manufactured by Kyoei Chemical Industry Co., Ltd.), OH equivalent 105, softening point: 100 ° C) 57.5 g was used as the hardening. Ingredients. Further, 0.7 g of a curing accelerator A and 2-methylimidazole (manufactured by Tokyo Chemical Industry Co., Ltd.) were used, and an epoxy resin composition was obtained by kneading. Using the epoxy resin composition, a cured test piece was obtained under the conditions of a molding temperature of 175 ° C, 3 minutes, a post-hardening temperature of 250 ° C, and 5 hours (forming condition A), and then a 5% weight loss temperature was measured. The results are shown in Table 1.

實施例2 Example 2

除了使用合成例8中獲得之環氧樹脂E 100g作為環氧樹脂成分以外,餘與實施例1同樣,測定5%重量減少溫度。結果示於表1。 A 5% weight loss temperature was measured in the same manner as in Example 1 except that 100 g of the epoxy resin E obtained in Synthesis Example 8 was used as the epoxy resin component. The results are shown in Table 1.

比較例1 Comparative example 1

除了使用合成例4中獲得之環氧樹脂B 100g作為環氧樹脂成分以外,餘與實施例1同樣,測定5%重量減少溫度。結果示於表1。 A 5% weight loss temperature was measured in the same manner as in Example 1 except that 100 g of the epoxy resin B obtained in Synthesis Example 4 was used as the epoxy resin component. The results are shown in Table 1.

比較例2 Comparative example 2

除了使用合成例6中獲得之環氧樹脂D 100g作為環氧樹脂成分以外,餘與實施例1同樣,測定5%重量減少溫度。結果示於表1。 A 5% weight loss temperature was measured in the same manner as in Example 1 except that 100 g of the epoxy resin D obtained in Synthesis Example 6 was used as the epoxy resin component. The results are shown in Table 1.

實施例3~15、比較例3、4 Examples 3 to 15, Comparative Examples 3 and 4

以表2~3所示之調配比例混練上述合成例中獲得之環氧樹脂A、E、或環氧樹脂C、硬化劑、無機填充劑及硬化促進劑(硬化觸媒)與其他添加劑,調製環氧樹脂組成物。表中之數值表示調配之重量份。 The epoxy resin A, E, or epoxy resin C, hardener, inorganic filler, hardening accelerator (hardening catalyst) and other additives obtained in the above synthesis examples are mixed and blended in the proportions shown in Tables 2 to 3. Epoxy resin composition. The values in the table indicate the parts by weight.

表中之簡寫說明 Abbreviation in the table

環氧樹脂C:鄰-甲酚酚醛清漆型環氧樹脂(環氧當量200,軟化點65℃。新日鐵化學公司製) Epoxy resin C: o-cresol novolac type epoxy resin (epoxy equivalent 200, softening point 65 ° C. manufactured by Nippon Steel Chemical Co., Ltd.)

(硬化劑) (hardener)

PN:酚酚醛清漆(PSM-4324,OH當量105、軟化點:100℃,群榮化學工業股份有限公司製) PN: phenol novolac (PSM-4324, OH equivalent 105, softening point: 100 ° C, manufactured by Qun Rong Chemical Industry Co., Ltd.)

TPM:三酚甲烷(TPM-100,OH當量97.5,軟化點105℃,群榮化學工業股份有限公司製) TPM: trisphenol methane (TPM-100, OH equivalent 97.5, softening point 105 ° C, manufactured by Qun Rong Chemical Industry Co., Ltd.)

(無機填充劑) (inorganic filler)

球狀二氧化系(FB-8S,電氣化學工業股份有限公司製) Spherical dioxide system (FB-8S, manufactured by Electric Chemical Industry Co., Ltd.)

(硬化促進劑) (hardening accelerator)

A:2-甲基咪唑(東京化成股份有限公司製) A: 2-methylimidazole (manufactured by Tokyo Chemical Industry Co., Ltd.)

B:2-苯基-4,5-二羥基甲基咪唑(2PHZ-PW,四國化成股份有限公司製) B: 2-phenyl-4,5-dihydroxymethylimidazole (2PHZ-PW, manufactured by Shikoku Chemicals Co., Ltd.)

C:參-(2,6-二甲氧基苯基)膦(東京化成股份有限公司製) C: ginseng-(2,6-dimethoxyphenyl)phosphine (manufactured by Tokyo Chemical Industry Co., Ltd.)

(矽烷偶合劑) (decane coupling agent)

4-胺基丙基乙氧基矽烷(KBR-903,信越化學工業股份有限公司製) 4-aminopropyl ethoxy decane (KBR-903, manufactured by Shin-Etsu Chemical Co., Ltd.)

(脫模劑) (release agent)

巴西棕櫚蠟(TOWAX 171,東亞化成股份有限公司製) Carnauba wax (TOWAX 171, manufactured by East Asia Chemical Co., Ltd.)

(著色劑) (Colorant)

碳黑(MA-100,三菱化學股份有限公司製) Carbon black (MA-100, manufactured by Mitsubishi Chemical Corporation)

使用該環氧樹脂組成物,以如下所示之成形條件進行成形。獲得硬化物試驗片後,供於各種物性測定。結果示於表2~3。 Using this epoxy resin composition, it was shaped by the molding conditions shown below. After obtaining a cured test piece, it was used for various physical properties. The results are shown in Tables 2 to 3.

成形條件 Forming conditions

A:成形溫度175℃、3分鐘,後硬化溫度250℃、5小時 A: forming temperature 175 ° C, 3 minutes, post-hardening temperature 250 ° C, 5 hours

B:成形溫度175℃、3分鐘,後硬化溫度175℃、5小時 B: forming temperature 175 ° C, 3 minutes, post-hardening temperature 175 ° C, 5 hours

1)環氧當量之測定 1) Determination of epoxy equivalent

使用電位差滴定裝置,使用甲基乙基酮作為溶劑,添加溴化四乙基銨乙酸溶液,以電位差滴定裝置,使用0.1mol/L過氯酸-乙酸溶液進行測定。 Using a potentiometric titration apparatus, methyl ethyl ketone was used as a solvent, and a tetraethylammonium bromide acetic acid solution was added thereto, and the mixture was measured by a potentiometric titration apparatus using a 0.1 mol/L perchloric acid-acetic acid solution.

2)熔融黏度 2) Melt viscosity

使用東亞工業股份有限公司製,CV-1S型錐板黏度計(cone-plate viscometer),在150℃進行測定。 The measurement was carried out at 150 ° C using a CV-1S cone-plate viscometer manufactured by East Asia Industrial Co., Ltd.

3)玻璃轉移點(Tg) 3) Glass transfer point (Tg)

利用SEIKO儀器製TMA6100型熱機械測定裝置,以升溫速度10℃/分鐘之條件求得Tg。 The Tg was determined under the conditions of a temperature increase rate of 10 ° C /min using a TMAKO instrument type TMA6100 thermomechanical measuring device.

4)長期熱分解安定性評價(重量保持率) 4) Long-term thermal decomposition stability evaluation (weight retention rate)

使用旋轉框恆溫器(TABAI ESPEC股份有限公司製,GPHH-201),由在250℃歷時1000小時後之試驗片重量與加熱前之試驗片重量之差求得重量保持率(wt%)。 The weight retention ratio (wt%) was determined from the difference between the weight of the test piece after 1000 hours at 250 ° C and the weight of the test piece before heating using a rotary frame thermostat (GPHH-201, manufactured by TABAI ESPEC Co., Ltd.).

5)螺旋式流動(spiral flow) 5) Spiral flow

依據規格(EMMI-1-66),在螺旋式流動之注入壓力(150Kgf/cm2)、硬化時間3分鐘之條件下以螺旋式流動測定用模具使環氧樹脂組成物成形,調查170℃下之流動長度。 According to the specification (EMMI-1-66), the epoxy resin composition was molded by a spiral flow measurement mold under the conditions of a spiral flow injection pressure (150 Kgf/cm 2 ) and a curing time of 3 minutes, and the temperature was investigated at 170 ° C. The length of the flow.

6)DSC發熱峰溫度 6) DSC heating peak temperature

利用SEIKO儀器製DSC6200型熱機械測定裝置,以升溫速度10℃/分鐘之條件求得發熱峰溫度。 The exothermic peak temperature was determined by a DSC6200 type thermomechanical measuring apparatus manufactured by SEIKO Instruments at a temperature rising rate of 10 ° C /min.

7)5%重量減少溫度 7) 5% weight reduction temperature

利用SEIKO儀器製TG/DTA 6200型熱機械測定裝置,在氮氣環境下,以升溫速度10℃/分鐘之條件求得5%重量減少溫度。 Using a TG/DTA 6200 type thermomechanical measuring apparatus manufactured by SEIKO Instruments, a 5% weight reduction temperature was obtained under a nitrogen atmosphere at a temperature increase rate of 10 ° C /min.

8)彎曲強度及彎曲彈性 8) Bending strength and bending flexibility

根據JISK 6911,以3點彎曲試驗法在常溫及250℃下 進行測定。 According to JIS K 6911, the 3-point bending test method is used at normal temperature and 250 ° C. The measurement was carried out.

9)彎曲強度.彈性率維持率 9) Flexural strength. Elasticity retention rate

求得高溫(250℃)時之彎曲強度及彎曲彈性率相對於常溫之彎曲強度及彎曲彈性率之維持率。愈高表示與室溫之物性變化愈少。 The bending strength and the bending elastic modulus at a high temperature (250 ° C) were obtained with respect to the bending strength and the bending elastic modulus at normal temperature. The higher the value, the less the change in physical properties with room temperature.

Claims (10)

一種以下述通式(2)表示之環氧樹脂, 在此,R獨立地表示氫原子或碳數1~6之烴基,G表示環氧丙基,n為重複數,包含10%以上n為1以上之多聚物。 An epoxy resin represented by the following formula (2), Here, R independently represents a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms, G represents a glycidyl group, and n is a repeating number, and 10% or more of n is a polymer of 1 or more. 一種環氧樹脂,其特徵係使以下述通式(1)表示,且以經膠體滲透層析所測定之面積%中n=1以上之成分為10%以上之多元羥基化合物與表氯醇反應而得, 在此,R獨立地表示氫原子或碳數1~6之烴基,G 表示環氧丙基,n表示重複數。 An epoxy resin characterized by being reacted with epichlorohydrin by a polyhydric hydroxy compound having a composition of % by weight or more and having a component of n = 1 or more as measured by colloidal permeation chromatography. And got it, Here, R independently represents a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms, G represents a glycidyl group, and n represents a repeating number. 一種環氧樹脂組成物,其特徵為含有如請求項2之環氧樹脂、酚系硬化劑、硬化觸媒及無機填充劑。 An epoxy resin composition comprising the epoxy resin according to claim 2, a phenolic curing agent, a curing catalyst, and an inorganic filler. 一種環氧樹脂組成物,其特徵為含有如請求項1之環氧樹脂、酚系硬化劑、硬化觸媒及無機填充劑。 An epoxy resin composition comprising the epoxy resin according to claim 1, a phenolic curing agent, a curing catalyst, and an inorganic filler. 如請求項3之環氧樹脂組成物,其中硬化觸媒係由咪唑類、有機膦類及胺類所組成群組選出之至少1種。 The epoxy resin composition of claim 3, wherein the hardening catalyst is at least one selected from the group consisting of imidazoles, organophosphines, and amines. 如請求項3之環氧樹脂組成物,其中硬化觸媒為以DSC在升溫速度10℃/分鐘之條件下測定環氧樹脂組成物時,發熱峰高點為150℃以上者。 The epoxy resin composition according to claim 3, wherein the curing catalyst is an epoxy resin composition measured at a temperature rising rate of 10 ° C /min by DSC, and the peak of the heat generation peak is 150 ° C or higher. 一種環氧樹脂組成物之硬化方法,其特徵係使如請求項3之環氧樹脂組成物於100℃~200℃成形後,於200℃~300℃進行後硬化(postcure)。 A method for curing an epoxy resin composition, characterized in that after the epoxy resin composition of claim 3 is formed at 100 ° C to 200 ° C, post-curing is carried out at 200 ° C to 300 ° C. 一種環氧樹脂硬化物,其特徵係使如請求項3之環氧樹脂組成物於100℃~200℃成形後,於200℃~300℃進行後硬化而得。 An epoxy resin cured product obtained by forming an epoxy resin composition according to claim 3 at 100 ° C to 200 ° C and then post-hardening at 200 ° C to 300 ° C. 如請求項8之環氧樹脂硬化物,其係半導體密封材用之環氧樹脂硬化物。 The cured epoxy resin of claim 8 which is an epoxy resin cured product for a semiconductor sealing material. 一種半導體裝置,其特徵係以如請求項9之環氧樹脂硬化物密封半導體元件而成。 A semiconductor device characterized by sealing a semiconductor element with an epoxy resin cured material as claimed in claim 9.
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