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CN1095728A - Epoxy resins and epoxy resin compositions - Google Patents

Epoxy resins and epoxy resin compositions Download PDF

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Publication number
CN1095728A
CN1095728A CN 94103299 CN94103299A CN1095728A CN 1095728 A CN1095728 A CN 1095728A CN 94103299 CN94103299 CN 94103299 CN 94103299 A CN94103299 A CN 94103299A CN 1095728 A CN1095728 A CN 1095728A
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Prior art keywords
epoxy resin
bisphenol
resin
novolak
epoxy
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CN 94103299
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CN1037972C (en
Inventor
安田清美
中村英夫
铃木照文
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Mitsui Chemical Industry Co Ltd
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Mitsui Petrochemical Industries Ltd
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Priority claimed from JP2882593A external-priority patent/JPH06239962A/en
Priority claimed from JP5028826A external-priority patent/JPH06239963A/en
Priority claimed from JP173194A external-priority patent/JPH07206978A/en
Application filed by Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Publication of CN1095728A publication Critical patent/CN1095728A/en
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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
    • C08G59/18Macromolecules 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
    • C08G59/22Di-epoxy compounds
    • C08G59/30Di-epoxy compounds containing atoms other than carbon, hydrogen, oxygen and nitrogen
    • 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
    • C08G59/02Polycondensates 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
    • C08G59/066Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols with chain extension or advancing agents
    • 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
    • C08G59/08Polycondensates containing more than one epoxy group per molecule of polyhydroxy compounds with epihalohydrins or precursors thereof of polyhydric phenols from phenol-aldehyde condensates
    • 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
    • C08G59/38Epoxy compounds containing three or more epoxy groups together with di-epoxy compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D163/00Coating compositions based on epoxy resins; Coating compositions based on derivatives of epoxy resins
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K1/00Printed circuits
    • H05K1/02Details
    • H05K1/03Use of materials for the substrate
    • H05K1/0313Organic insulating material
    • H05K1/032Organic insulating material consisting of one material
    • H05K1/0326Organic insulating material consisting of one material containing O

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Epoxy Resins (AREA)
  • Reinforced Plastic Materials (AREA)

Abstract

An epoxy resin prepared by glycidyl etherification of bisphenol (1) and a novolak resin (II) with an epihalohydrin or a methylepihalohydrin in the presence of optionally halogenated bisphenol (III); and an epoxy resin composition prepared by further reacting the thus-obtained epoxy resin with a halogenated bisphenol (III), the product of the present invention is suitable for processing, and after curing, exhibits excellent heat resistance, blister resistance and copper clad laminate adhesion.

Description

本发明涉及一种环氧树脂和一种包括所说环氧树脂的环氧树脂组合物。特别是,本发明涉及一种在与固化剂混合时呈现低粘度因而能方便成型的环氧树脂,并且,该树脂一旦固化后,就具有优异的耐热性和高的机械强度。本发明也涉及一种环氧树脂组合物,它对诸如玻璃布这类材料呈现极好的浸渍性,而且,一旦固化后,该组合物就呈现高耐热性和耐起泡性因而能用于生产印刷电路板,尤其是多层印刷电路板用铜包层环氧树脂层压板中。The present invention relates to an epoxy resin and an epoxy resin composition comprising said epoxy resin. In particular, the present invention relates to an epoxy resin which exhibits low viscosity when mixed with a curing agent so as to facilitate molding, and which, once cured, has excellent heat resistance and high mechanical strength. The present invention also relates to an epoxy resin composition which exhibits excellent impregnation properties for materials such as glass cloth and which, once cured, exhibits high heat resistance and resistance to blistering so that it can be used Used in the production of printed circuit boards, especially copper-clad epoxy laminates for multilayer printed circuit boards.

通过混合塑料材料基料和补强剂而制备的塑料复合材料因其具有优良的耐热性、耐候性、耐化学性、或机械强度从而广泛用于工业中。环氧树脂因其具有良好的动态性质而广泛用作塑料复合材料的基料,它们并且可以极强地粘合用作补强剂的增强纤维,所得的复合材料是易于成型的。A plastic composite material prepared by mixing a plastic material base and a reinforcing agent is widely used in industry because of its excellent heat resistance, weather resistance, chemical resistance, or mechanical strength. Epoxy resins are widely used as binders for plastic composites due to their good dynamic properties, they can also extremely strongly bond reinforcing fibers used as reinforcements, and the resulting composites are easily formable.

在所述塑料复合材料中,人们极期望含有鉴于具有优良的耐热性和机械强度的环氧树脂和碳纤维的那种复合材料,将成为最显著的用于宇肮、汽车和其它高科技工业的下一代结构材料。Among the plastic composite materials, it is highly expected that the composite material containing epoxy resin and carbon fiber in view of its excellent heat resistance and mechanical strength will become the most prominent application in the aerospace, automobile and other high-tech industries. next-generation structural materials.

然而,人们期望这些复合材料具有更高的耐热性和进一步改进的成型性或可模塑性以使它们能够用作这些高科技领域的结构材料。However, these composite materials are expected to have higher heat resistance and further improved formability or moldability to enable them to be used as structural materials in these high-tech fields.

近年来,电子设备的范围已大大地扩大,多层印刷电路板不仅在计算机相关的设备中,而且在自动控制机器、通信设备、商业装置、游戏机等等中正在寻找它们的应用,这是由于它们的性能得到改进,尺寸减小所致。In recent years, the range of electronic equipment has greatly expanded, and multilayer printed circuit boards are finding their application not only in computer-related equipment but also in automatic control machines, communication equipment, business equipment, game machines, etc., which are Due to their improved performance, the size has been reduced.

另一方面,在计算机领域,系统结构已经历了明显的变化正如经常被认为的下降趋势工作场所周围而构制的分配系统已很普通。用在这种分配系统中的印刷电路板在提高叠层产品的层数方面还没有开发,这些电路板通常包括4至10层的叠层产品。在印刷电路板这一领域,能实现高密度包装的良好式样以及厚度的减小正在调查研究之中。In the computer field, on the other hand, system architecture has undergone marked changes as is often perceived as a downward trend around the workplace where structured distribution systems have become commonplace. Printed circuit boards used in such dispensing systems have not been developed to increase the number of layers of laminated products, and these circuit boards generally include laminated products with 4 to 10 layers. In the field of printed circuit boards, good form factors that enable high-density packaging and reduction in thickness are being investigated.

为了适合施于印刷电路板的这些要求,印刷电路板的基材就应更加改进耐热性和耐起泡性。In order to meet these requirements imposed on printed circuit boards, the base material of printed circuit boards should be more improved in heat resistance and blister resistance.

现有技术中改进环氧树脂耐热性的已知方法之一是加入多官能环氧树脂从而提高该树脂的交联密度。酚醛清漆(Novolak)环氧树脂由于其价格不贵而被广泛用于这种改性。One of the methods known in the prior art to improve the heat resistance of epoxy resins is to add multifunctional epoxy resins to increase the crosslink density of the resins. Novolak epoxy resins are widely used for this modification due to their inexpensiveness.

然而,Novolak环氧树脂有相当宽的分子量分布,当大量加入Novolak环氧树脂时,或当使用高分子量的Novolak环氧树脂时,所得的树脂具有过高的粘度。当这种高粘度的树脂被用作塑料复合材料的基料时,很难用该基料树脂完全浸渍增强纤维而且很难成型所得的塑料复合材料。另外,仅仅加入多官能环氧树脂也不能满足施于印刷电路板用叠层产品的耐热性的严格要求。例如,通过过量加入这种多官能环氧树脂而对耐热性的改进将导致该组合物硬化变脆,而当用这种组合物制备的叠层产品在煮沸后进行焊接时,经常出现脱层而导致起泡。However, Novolak epoxy resin has a rather broad molecular weight distribution, and when Novolak epoxy resin is added in a large amount, or when a high molecular weight Novolak epoxy resin is used, the resulting resin has an excessively high viscosity. When such a high-viscosity resin is used as a base for plastic composites, it is difficult to completely impregnate reinforcing fibers with the base resin and shape the resulting plastic composite. In addition, mere addition of a multifunctional epoxy resin cannot satisfy the strict heat resistance requirements imposed on laminated products for printed circuit boards. For example, the improvement of heat resistance by excessive addition of this multifunctional epoxy resin will cause the composition to harden and become brittle, and when the laminated product prepared with this composition is soldered after boiling, delamination often occurs. layer resulting in blistering.

本发明的第一个目的是提供一种易于成型的环氧树脂,当与固化剂混合时呈现低粘度,而且一旦固化后就呈现优良的耐热性以及高的机械强度。A first object of the present invention is to provide an epoxy resin that is easy to mold, exhibits low viscosity when mixed with a curing agent, and exhibits excellent heat resistance and high mechanical strength once cured.

本发明的第二个目的是提供一种环氧树脂组合物,它对诸如玻璃布之类的材料呈现优良的浸渍性,而且它一旦固化后,呈现优良的耐热性耐起泡性,和对铜包层的粘合性,因此,它特别适用于制备印刷电路板用的铜包层环氧树脂层压制品,尤其是多层印刷电路板的层压制品。A second object of the present invention is to provide an epoxy resin composition which exhibits excellent impregnation properties to materials such as glass cloth and which, once cured, exhibits excellent heat resistance and blister resistance, and Adhesion to copper cladding, therefore, it is particularly suitable for the preparation of copper clad epoxy laminates for printed circuit boards, especially laminates for multilayer printed circuit boards.

本发明的发明人已进行了充分的研究以实现上述第一个目的,并且找到了一种易于成型的低粘度环氧树脂,它一旦固化后就呈现优良的耐热性以及高机械强度,该树脂可通过一种双酚与一种表卤代醇或一种甲基表卤代醇在一种novolak树脂存在下进行缩水甘油基醚化作用从而同时进行双酚和novolak树脂的缩水甘油基醚化作用而制备。The inventors of the present invention have conducted sufficient research to achieve the above-mentioned first object, and have found an easily moldable low-viscosity epoxy resin that exhibits excellent heat resistance and high mechanical strength once cured, which Resins can be glycidyl etherified simultaneously with bisphenols and novolak resins by glycidyl etherification of a bisphenol with an epihalohydrin or a methylepihalohydrin in the presence of a novolak resin prepared by chemical reaction.

要实现上述本发明的第一个目的,根据本发明提供一种环氧树脂(A),它是通过将双酚(Ⅰ)和novolak树脂(Ⅱ)用至少选自表卤代醇和甲基表卤代醇之一进行缩水甘油基醚化作用而制备的。To achieve the above-mentioned first object of the present invention, the present invention provides an epoxy resin (A), which is obtained by using bisphenol (I) and novolak resin (II) with at least one selected from epihalohydrin and methyl epihalohydrin One of the halogenated alcohols is prepared by glycidyl etherification.

此外,为了要实现本发明的上述第二个目的,根据本发明要提供一种主要含有加聚合物(polyadduct)环氧树脂(B)的环氧树脂组合物,该环氧树脂(B)是将双酚(Ⅰ)和novolak树脂(Ⅱ)与至少选自表卤代醇和甲基表卤代醇之一进行缩水甘油基醚化作用以形成环氧树脂(A),然后在一种鎓盐或碱性催化剂存在下将环氧树脂(A)与一种卤代双酚(Ⅲ)进行反应生产加聚合物树脂(B)而制备。In addition, in order to achieve the above-mentioned second object of the present invention, according to the present invention, an epoxy resin composition mainly containing polyadduct epoxy resin (B) will be provided, and the epoxy resin (B) is Glycidyl etherification of bisphenol (I) and novolak resin (II) with at least one selected from epihalohydrin and methyl epihalohydrin to form epoxy resin (A), and then in an onium salt Or in the presence of a basic catalyst, the epoxy resin (A) is reacted with a halogenated bisphenol (Ⅲ) to produce the polymer resin (B).

更进一步,为了实现本发明的上述第二个目的,根据本发明还提供一种主要含有加聚合物环氧树脂(D)的环氧树脂组合物,该环氧树脂(D)是将双酚(Ⅰ),novolak树脂(Ⅱ),和卤代双酚(Ⅲ)与表卤代醇或甲基表卤代醇进行缩水甘油基醚化作用形成环氧树脂(C),然后在一种鎓盐或碱性催化剂存在下将环氧树脂(A)与一种卤代双酚(Ⅲ)进行反应产生加聚合物树脂(D)而制备。Furthermore, in order to achieve the above-mentioned second object of the present invention, according to the present invention, there is also provided an epoxy resin composition mainly containing polymer-added epoxy resin (D), the epoxy resin (D) being bisphenol (I), novolak resin (II), and halogenated bisphenol (III) undergo glycidyl etherification with epihalohydrin or methyl epihalohydrin to form epoxy resin (C), and then in an onium It is prepared by reacting an epoxy resin (A) with a halogenated bisphenol (III) in the presence of a salt or a basic catalyst to produce an added polymer resin (D).

以下详细叙述本发明的环氧树脂以及含有所述环氧树脂的环氧树脂组合物。The epoxy resin of the present invention and the epoxy resin composition containing the epoxy resin will be described in detail below.

本发明的环氧树脂(A)是用双酚(Ⅰ)和酚醛清漆(novolak)树脂(Ⅱ)作为原料而生产的。本发明的环氧树脂组合物主要含有加聚合物环氧树脂(B)或(D),环氧树脂(B)或(D)分别是由环氧树脂(A)或(C)与卤化的二酚(Ⅲ)进行加聚反应而制成的,而环氧树脂(A)或(C)则是通过双酚(Ⅰ),novolak树脂(Ⅱ),以及卤代双酚(Ⅲ)的缩水甘油基醚化作用而制备的。The epoxy resin (A) of the present invention is produced by using bisphenol (I) and novolak resin (II) as raw materials. The epoxy resin composition of the present invention mainly contains the addition polymer epoxy resin (B) or (D), and epoxy resin (B) or (D) is respectively made of epoxy resin (A) or (C) and halogenated Diphenol (Ⅲ) is prepared by polyaddition reaction, while epoxy resin (A) or (C) is obtained by shrinking bisphenol (I), novolak resin (II), and halogenated bisphenol (Ⅲ) Glyceryl etherification and preparation.

双酚(Ⅰ)Bisphenol (I)

用作制备环氧树脂(A)或(C)的原料双酚(Ⅰ)是由通式(ⅰ)表示的化合物:The bisphenol (I) used as the raw material for preparing epoxy resin (A) or (C) is a compound represented by the general formula (i):

其中R是二价基,它选自-CH2-,-CHCH3-,-C(CH32-,-SO2-,

Figure 94103299X_IMG2
,和-C(CH3)(C6H5)-;R1单独选自氢原子和含有1至5个碳原子的烃;n是0至4的整数。双酚(Ⅰ)的示范例包括双酚A,双酚F,和双酚AD。其中最优选的是双酚A,它是在上述分子式(ⅰ)中R是异亚丙基,R1是氢原子的双酚。wherein R is a divalent group selected from -CH 2 -, -CHCH 3 -, -C(CH 3 ) 2 -, -SO 2 -,
Figure 94103299X_IMG2
, and -C(CH 3 )(C 6 H 5 )-; R 1 is independently selected from hydrogen atoms and hydrocarbons containing 1 to 5 carbon atoms; n is an integer of 0 to 4. Exemplary bisphenols (I) include bisphenol A, bisphenol F, and bisphenol AD. Among them, bisphenol A is most preferred, which is a bisphenol in the above formula (i) in which R is isopropylidene and R 1 is a hydrogen atom.

Novolak树脂(Ⅱ)Novolak resin (Ⅱ)

用于制备本发明的环氧树脂(A)或环氧树脂(C)(A)或(C)用于制备本发明的环氧树脂组合物)的novolak树脂(Ⅱ)是甲醛和以上所述的双酚(Ⅰ)或是由以下的通式(ⅱ)表示的酚的缩合产物:The novolak resin (II) used to prepare the epoxy resin (A) or epoxy resin (C) of the present invention (A) or (C) for the preparation of the epoxy resin composition of the present invention) is formaldehyde and the above-mentioned Bisphenol (I) or a condensation product of phenol represented by the following general formula (ii):

Figure 94103299X_IMG3
Figure 94103299X_IMG3

其中R1和R2各自选自氢原子和含有1至10个碳原子的烃。由通式(ⅱ)所表示的优选的酚的示范例包括酚,邻甲酚,对-叔辛基酚,和对甲酚。wherein R1 and R2 are each selected from a hydrogen atom and a hydrocarbon containing 1 to 10 carbon atoms. Examples of preferred phenols represented by the general formula (ii) include phenol, o-cresol, p-tert-octylphenol, and p-cresol.

可与甲醛缩合形成novolak树脂(Ⅱ)的双酚(Ⅰ)可以是由通式(ⅰ)表示的双酚。用于制备novolak树脂(Ⅱ)的双酚(Ⅰ)优选为双酚A或双酚AD。The bisphenol (I) which can be condensed with formaldehyde to form the novolak resin (II) may be a bisphenol represented by the general formula (i). The bisphenol (I) used in the preparation of novolak resin (II) is preferably bisphenol A or bisphenol AD.

Novolak树脂(Ⅱ)可优选具有高达100℃的软化点,更优选的软化点范围从30至100℃。当使用超过110℃的软化点的双酚(Ⅱ)来制备环氧树脂时,所得环氧树脂由于其过高含量的高分子量物质,从而,过高的粘度而不易成型。当所述环氧树脂进一步与卤代双酚(Ⅲ)反应来制备环氧树脂(B)或(D)时,所得的树脂将会有过高含量的高分子量物质而导致不能充分浸渍到玻璃布中。The Novolak resin (II) may preferably have a softening point up to 100°C, more preferably a softening point ranging from 30 to 100°C. When bisphenol (II) having a softening point exceeding 110°C is used to prepare an epoxy resin, the resulting epoxy resin is not easily moldable due to its excessively high content of high molecular weight substances, and thus, excessively high viscosity. When the epoxy resin is further reacted with halogenated bisphenol (III) to prepare epoxy resin (B) or (D), the resulting resin will have an excessively high content of high molecular weight substances, resulting in insufficient impregnation into the glass cloth.

Novolak树脂(Ⅱ)的数均分子量优选为300-1000,更优选300-700,进一步优选为350-600。最好是novolak树脂(Ⅱ)的分子量分布高达2,更好的是1.1至1.8。本发明所用的术语,分子量分布表示重均分子量对数均分子量的比值,即Mw/Mn。The number average molecular weight of the Novolak resin (II) is preferably 300-1000, more preferably 300-700, still more preferably 350-600. Preferably the novolak resin (II) has a molecular weight distribution up to 2, more preferably from 1.1 to 1.8. As the term used in the present invention, molecular weight distribution means the ratio of weight average molecular weight to number average molecular weight, ie Mw/Mn.

Novolak树脂(Ⅱ)可通过以上所述的双酚和/或酚与甲醛可在有或无诸如二甲苯或甲苯之类溶剂条件下,并在酸性催化剂存在下进行反应而制备。可以使用多聚甲醛代替甲醛。甲醛的用量为每摩尔全部双酚和/或酚0.2至0.8摩尔从而使软化点和平均分子量最佳化。Novolak resin (II) can be prepared by reacting the above-mentioned bisphenol and/or phenol with formaldehyde with or without a solvent such as xylene or toluene, and in the presence of an acidic catalyst. Paraformaldehyde can be used instead of formaldehyde. Formaldehyde is used in an amount of 0.2 to 0.8 moles per mole of total bisphenols and/or phenols to optimize softening point and average molecular weight.

在上述的反应中使用溶剂时,其所用的比例为每100%(重量)的全部所述双酚和/或酚的20至100%(重量)。When the solvent is used in the above reaction, it is used in a proportion of 20 to 100% by weight per 100% by weight of the total of said bisphenol and/or phenol.

所用的酸性催化剂典型的可以是诸如硫酸、盐酸、硝酸、或磷酸之类的无机酸;或者是诸如对甲苯磺酸或草酸之类有机酸。在这些酸中,对甲苯磺酸由于其高酸性和与反应基质良好的混溶性因此是优选的。酸性催化剂所用比例优选为每100%(重量)全部所述的双酚和/或酚的0.05至2%(重量)。更优选0.1至1%(重量)。使用极少量的酸性催化剂会导致反应失败,从而不能生产出所需的分子量的novolak树脂(Ⅱ)。使用极过量的酸性催化剂将导致很难控制反应,并导致所得novolak树脂过高的分子量。The acidic catalyst used may typically be an inorganic acid such as sulfuric acid, hydrochloric acid, nitric acid, or phosphoric acid; or an organic acid such as p-toluenesulfonic acid or oxalic acid. Among these acids, p-toluenesulfonic acid is preferred due to its high acidity and good miscibility with the reaction matrix. The acidic catalyst is preferably used in a proportion of 0.05 to 2% by weight per 100% by weight of all said bisphenols and/or phenols. More preferably 0.1 to 1% by weight. The use of very small amounts of acidic catalysts can lead to failure of the reaction to produce the desired molecular weight novolak resin (II). The use of an extreme excess of acidic catalyst will result in difficult control of the reaction and lead to excessively high molecular weight of the resulting novolak resin.

该反应一般可通过在1.5至4小时内把反应混合物加热至70至100℃的温度,然后加热至100至120℃的温度以便脱水缩合。该脱水缩合或在减压下得到促进或利用在诸如二甲苯或甲苯之类溶剂中共沸回流并除去缩合的水而促进该缩合反应。该反应最好继续到不再产生缩合的水时为止。该反应一般进行3至5个小时。The reaction can generally be carried out by heating the reaction mixture to a temperature of 70 to 100°C for 1.5 to 4 hours and then to a temperature of 100 to 120°C for dehydration condensation. The dehydration condensation is either promoted under reduced pressure or by azeotropic reflux in a solvent such as xylene or toluene and removal of the water of condensation. The reaction is preferably continued until no more water of condensation is produced. The reaction is generally carried out for 3 to 5 hours.

反应完成后以所用酸性催化剂化学计算当量的碱化合物加到反应混合物中从而中和酸性催化剂。可以使用的典型碱化合物包括氢氧化钠,氢氧化钾,和三乙醇胺吗啉。另一方面,可在反应混合物加入无水溶剂形成均匀的溶液,然后用一碱的水溶液洗涤该溶液来进行中和作用。After the reaction is complete, a stoichiometric equivalent of the acidic catalyst used is added to the reaction mixture to neutralize the acidic catalyst. Typical base compounds that can be used include sodium hydroxide, potassium hydroxide, and triethanolamine morpholine. Alternatively, neutralization can be carried out by adding an anhydrous solvent to the reaction mixture to form a homogeneous solution, and then washing the solution with an aqueous base solution.

当用溶剂来生产novolak树脂(Ⅱ)时,所用的溶剂被蒸馏出而留下novolak树脂。When a solvent is used to produce the novolak resin (II), the used solvent is distilled off to leave the novolak resin.

在含有3个或更多官能度的novolak树脂(Ⅱ)中多核组分可以优选构成双酚(Ⅰ)和novolak树脂(Ⅱ)中酚组分的3至50%(重量),更优选5至40%(重量)以提供环氧树脂(A)或双酚(Ⅰ),而novolak树脂(Ⅱ)和卤代双酚(Ⅲ)以提供环氧树脂(C)。当所述多核组分的含量小于3%(重量)时,所得环氧树脂固化后的玻璃化转变温度将不能得到足够改进。另一方面,当多核组分的含量超过50%(重量)时,通过其后的环氧树脂(A)或(C)与卤代双酚(Ⅲ)的反应而制成的环氧树脂(B)或(D)将具有过高的分子量导致不能充分浸渍到玻璃布内。In novolak resins (II) containing 3 or more functionalities, the polynuclear components may preferably constitute bisphenols (I) and 3 to 50% by weight of the phenolic components in novolak resins (II), more preferably 5 to 40% by weight to provide epoxy resin (A) or bisphenol (I), and novolak resin (II) and halogenated bisphenol (III) to provide epoxy resin (C). When the content of the multi-core component is less than 3% by weight, the glass transition temperature of the resulting epoxy resin after curing will not be sufficiently improved. On the other hand, when the content of the multinuclear component exceeds 50% by weight, the epoxy resin ( B) or (D) would have too high a molecular weight to sufficiently impregnate into the glass cloth.

卤代双酚(Ⅲ)Halogenated bisphenol (Ⅲ)

用作制备环氧树脂(C)原料的卤代双酚(Ⅲ)最好是溴代双酚。最优选的是四溴双酚A,四溴双酚F,和1,1-双(3,5-二溴-4-羟苯基)乙烷。The halogenated bisphenol (III) used as a raw material for the preparation of the epoxy resin (C) is preferably brominated bisphenol. Most preferred are tetrabromobisphenol A, tetrabromobisphenol F, and 1,1-bis(3,5-dibromo-4-hydroxyphenyl)ethane.

缩水甘油化反应Glycidylation reaction

双酚(Ⅰ)和novolak树脂(Ⅱ)与表卤代醇或甲基表卤代醇生成环氧树脂(A)的反应;双酚(Ⅰ),novolak树脂(Ⅱ)和卤代双酚(Ⅲ)与表卤代醇或甲基表卤代醇生成环氧树脂(C)的反应可根据各种已知方法来实现。然而,为了提供具有可靠质量的生成缩水甘油基醚化环氧树脂(A)或(C),最好顺序地进行醚化步骤和脱卤化氢步骤。表卤代醇优选表氯醇,而甲基表卤代醇优选是2-甲基表氯醇。Reaction of bisphenol (I) and novolak resin (II) with epihalohydrin or methyl epihalohydrin to generate epoxy resin (A); bisphenol (I), novolak resin (II) and halogenated bisphenol ( iii) The reaction with epihalohydrin or methylepihalohydrin to form epoxy resin (C) can be carried out according to various known methods. However, in order to provide the resulting glycidyl etherified epoxy resin (A) or (C) with reliable quality, it is preferable to carry out the etherification step and the dehydrohalogenation step sequentially. The epihalohydrin is preferably epichlorohydrin, and the methylepihalohydrin is preferably 2-methylepichlorohydrin.

醚化步骤可以醚化催化剂存在下进行,其用量为双酚(Ⅰ)和novolak树脂(Ⅱ)混合物,或双酚(Ⅰ),novolak树脂(Ⅱ)和卤代双酚(Ⅲ)的混合物中每1当量酚羟基0.1至5%(摩尔)。典型的醚化催化剂包括叔胺例如三甲胺,三乙胺等等;叔膦例如三苯基膦,三丁基膦等;季铵盐例如氯化四甲铵,溴化四甲铵,氯化四乙铵,胆碱盐酸盐等;季磷鎓盐例如四甲基鏻溴化物,四甲基鏻碘化物,四苯基鏻溴化物,三苯基丙基鏻溴化物,等;叔锍盐例如氯化苄基二丁基锍,氯化苄基二甲基锍,等;和无机碱例如氢氧化钠,氢氧化钾等。其中优选的是氯化四甲基铵。The etherification step can be carried out in the presence of an etherification catalyst, and its dosage is a mixture of bisphenol (I) and novolak resin (II), or a mixture of bisphenol (I), novolak resin (II) and halogenated bisphenol (III) 0.1 to 5% (mol) per 1 equivalent of phenolic hydroxyl group. Typical etherification catalysts include tertiary amines such as trimethylamine, triethylamine, etc.; tertiary phosphines such as triphenylphosphine, tributylphosphine, etc.; quaternary ammonium salts such as tetramethylammonium chloride, tetramethylammonium bromide, Tetraethylammonium, choline hydrochloride, etc.; quaternary phosphonium salts such as tetramethylphosphonium bromide, tetramethylphosphonium iodide, tetraphenylphosphonium bromide, triphenylpropylphosphonium bromide, etc.; tertiary sulfonium salts such as benzyldibutylsulfonium chloride, benzyldimethylsulfonium chloride, etc.; and inorganic bases such as sodium hydroxide, potassium hydroxide and the like. Of these, tetramethylammonium chloride is preferred.

在醚化步骤中,该反应一直进行到至少50%(摩尔),优选至少70%(摩尔)的酚羟基被醚化为止。一般该反应在惰性气氛中于60-110℃的温度下进行1至12小时。该系统中水的含量最好保持不多于3.0%(重量)。In the etherification step, the reaction is carried out until at least 50 mole percent, preferably at least 70 mole percent, of the phenolic hydroxyl groups are etherified. Generally the reaction is carried out in an inert atmosphere at a temperature of 60-110°C for 1 to 12 hours. The water content in the system is preferably kept at not more than 3.0% by weight.

下一脱卤化氢步骤可在醚化步骤所得含有未反应的表卤代醇反应产物中进行。在该反应中,优选使用醚化步骤中所用的那些碱化合物,例如碱金属氢氧化物作为催化剂。在脱卤化氢步骤中,一般碱化合物用量为每1当量novolak树脂(Ⅱ)的酚羟基0.5摩尔或更多,优选0.8摩尔或更多,优选每1当量酚羟基使用高达1摩尔的碱化合物使反应产物不便于凝胶化。该反应一般在60-100℃温度下进行1-3小时。当使用氢氧化钠时,最好通过除去副产物水情况下进行该反应。除去水可通过反应混合物的脱水,例如表卤代醇-水的共沸,并把表卤代醇回复到该反应系统来实现。反应完成后,本发明的环氧树脂可经后步处理后而制得,该后步处理是指例如通过真空蒸馏除去未反应的表卤代醇,通过水洗处理除去副产物盐,并且可有可无用磷酸这样的弱酸或磷酸二氢钠中和反应混合物来进行后处理,以及过滤和干燥。此外,如果需要减少可水解氯的用量,可再进行第二次脱卤化氢。用于减少可水解氯的量的碱化合物比例为每1摩尔残留的可水解氯1至3摩尔。优选为1.2至3摩尔。该反应于60-100℃的温度下进行约1-3小时。该反应可以用或不用溶剂进行。用溶剂时,优选的是二甲苯、甲苯、甲乙酮(MEK)、甲基·异丁基酮。The next dehydrohalogenation step can be carried out on the reaction product obtained from the etherification step which contains unreacted epihalohydrin. In this reaction, those alkali compounds used in the etherification step, such as alkali metal hydroxides, are preferably used as catalysts. In the dehydrohalogenation step, the general amount of alkali compound used is 0.5 mole or more per 1 equivalent of the phenolic hydroxyl group of novolak resin (II), preferably 0.8 mole or more, preferably up to 1 mole of alkali compound per 1 equivalent of phenolic hydroxyl group. The reaction product is not easy to gel. The reaction is generally carried out at a temperature of 60-100°C for 1-3 hours. When sodium hydroxide is used, the reaction is preferably carried out with removal of by-product water. Removal of water can be achieved by dehydration of the reaction mixture, such as epihalohydrin-water azeotrope, and returning epihalohydrin to the reaction system. After the reaction is completed, the epoxy resin of the present invention can be prepared after post-processing, which refers to, for example, removing unreacted epihalohydrins by vacuum distillation, removing by-product salts by water washing, and may have The workup can be carried out by neutralizing the reaction mixture with a weak acid such as phosphoric acid or sodium dihydrogen phosphate, as well as filtering and drying. In addition, if it is necessary to reduce the amount of hydrolyzable chlorine, a second dehydrohalogenation can be carried out. The ratio of the alkali compound for reducing the amount of hydrolyzable chlorine is 1 to 3 moles per 1 mole of residual hydrolyzable chlorine. Preferably it is 1.2 to 3 moles. The reaction is carried out at a temperature of 60-100°C for about 1-3 hours. The reaction can be performed with or without a solvent. When a solvent is used, preferred are xylene, toluene, methyl ethyl ketone (MEK), and methyl isobutyl ketone.

在环氧树脂(A)的制备中,所用双酚(Ⅰ)和novolak树脂(Ⅱ)的重量比为1-99∶99-5,优选为5-95∶95-5,更优选为10-90∶90-10。当使用过量的novolak组分时,所得环氧树脂将具有过高含量的较高分子量物质,例如它在预浸制作物时将不能充分浸渍到玻璃布内,结果,所得的层压制品耐冲击性差。当novolak树脂(Ⅱ)的比例过低时,所得环氧树脂将不具有足够的耐热性。In the preparation of epoxy resin (A), the weight ratio of used bisphenol (I) and novolak resin (II) is 1-99:99-5, preferably 5-95:95-5, more preferably 10- 90:90-10. When an excess of the novolak component is used, the resulting epoxy resin will have an excessively high content of higher molecular weight species, for example it will not be sufficiently impregnated into the glass cloth during prepreg, and as a result, the resulting laminate will be impact resistant Poor sex. When the proportion of novolak resin (II) is too low, the resulting epoxy resin will not have sufficient heat resistance.

对于耐热的复合材料,所用双酚(Ⅰ)和novolak树脂(Ⅱ)的重量比为50-90∶50∶10,优选为65-90∶35-10。当novolak树脂(Ⅱ)的比例过低时,所得环氧树脂将不具备足够的耐热性。当novolak组分使用过量时,所得环氧树脂将具有过高的粘度并不易成型。For heat-resistant composite materials, the weight ratio of bisphenol (I) and novolak resin (II) used is 50-90:50:10, preferably 65-90:35-10. When the proportion of novolak resin (II) is too low, the resulting epoxy resin will not have sufficient heat resistance. When the novolak component is used in excess, the resulting epoxy resin will have too high a viscosity and is not easy to shape.

在环氧树脂(C)的生产中,所用双酚(Ⅰ),novolak树脂(Ⅱ)和卤代双酚(Ⅲ)的重量比为5-80∶94-5∶1-15,优选为7-80∶90-10∶3-10。In the production of epoxy resin (C), used bisphenol (I), the weight ratio of novolak resin (II) and halogenated bisphenol (III) is 5-80: 94-5: 1-15, preferably 7 -80:90-10:3-10.

由上述反应制备的缩水甘油基醚化环氧树脂(A)具有170-220克/当量的环氧当量,而且用于印刷电路板时,它最好具有高达50℃软化点,170-220克/当量的环氧当量,卤化物含量高达0.1%(重量)。由上述反应生产的缩水甘油基醚化的环氧树脂(C)具有高达40℃的软化点,170-220克/当量的环氧当量,卤化物含量高达10%(重量)。The glycidyl etherified epoxy resin (A) prepared by the above reaction has an epoxy equivalent of 170-220 g/equivalent, and when used for printed circuit boards, it preferably has a softening point as high as 50°C, 170-220 g / equivalent of epoxy equivalent, halide content up to 0.1% (weight). The glycidyl etherified epoxy resin (C) produced by the above reaction has a softening point as high as 40°C, an epoxy equivalent of 170-220 g/equivalent, and a halide content as high as 10% by weight.

加聚反应Polyaddition reaction

加聚合物树脂(B)和(D)分别是本发明环氧树脂组合物的主要成分,树脂(B)和(D)分别是由环氧树脂(A)和(C)与卤化双酚(Ⅲ)进行反应而制造的。Adding polymer resin (B) and (D) is the main component of epoxy resin composition of the present invention respectively, and resin (B) and (D) are respectively made of epoxy resin (A) and (C) and halogenated bisphenol ( Ⅲ) Manufactured by reaction.

环氧树脂(A)或(B)与卤代双酚(Ⅲ)的加聚反应是在惰性气氛内在可有或无诸如季铵盐或季锍盐之类催化剂存在下,(其用量为10-30ppm),于120℃~170℃的温度经4-15小时而实现的。The polyaddition reaction of epoxy resin (A) or (B) and halogenated bisphenol (Ⅲ) is in inert atmosphere with or without the presence of catalysts such as quaternary ammonium salt or quaternary sulfonium salt, (its consumption is 10 -30ppm), realized after 4-15 hours at a temperature of 120°C to 170°C.

该反应可在诸如甲苯、二甲苯和环己烷之类溶剂中进行,以致使反应混合物中固体含量高达30%(重量)。The reaction can be carried out in solvents such as toluene, xylene and cyclohexane so that the solids content of the reaction mixture can be as high as 30% by weight.

可用于加聚反应的卤代双酚(Ⅲ)可与缩水甘油基醚化中所用的那些卤代双酚相同。在这些卤代双酚(Ⅲ)中,优选是溴代双酚,尤其是四溴化双酚A,四溴化双酚F,和1,1-双(3,5-二溴-4-羟苯基)乙烷。The halogenated bisphenols (III) usable in the polyaddition reaction may be the same as those used in the glycidyl etherification. Among these halogenated bisphenols (III), brominated bisphenols are preferred, especially tetrabrominated bisphenol A, tetrabrominated bisphenol F, and 1,1-bis(3,5-dibromo-4- hydroxyphenyl) ethane.

在环氧树脂(A)与卤代双酚(Ⅲ)的反应生成加聚合物环氧树脂(B)中,环氧树脂(A)和卤代双酚(Ⅲ)的优选用量比为74∶26至55∶45。在环氧树脂(C)与卤代双酚(Ⅲ)的反应生成加聚合物环氧树脂(D)中,环氧树脂(C)和卤代双酚(Ⅲ)的优选用量比为90∶10至58∶42。当使用过量的卤代双酚(Ⅲ)时,将过量形成高分子量物质,这将导致在制作预浸物时树脂组合物不能充分浸渍到布内。当卤代双酚(Ⅲ)的比例过低时,所得环氧树脂组合物将不具有足够的阻燃性。In the reaction of epoxy resin (A) and halogenated bisphenol (Ⅲ) to generate polymer epoxy resin (B), the preferred amount ratio of epoxy resin (A) and halogenated bisphenol (Ⅲ) is 74: 26 to 55: 45. In the reaction of epoxy resin (C) and halogenated bisphenol (Ⅲ) to generate polymer epoxy resin (D), the preferred amount ratio of epoxy resin (C) and halogenated bisphenol (Ⅲ) is 90: 10 to 58:42. When an excessive amount of the halogenated bisphenol (III) is used, a high molecular weight substance will be formed in excess, which will result in insufficient impregnation of the resin composition into the cloth when making a prepreg. When the proportion of halogenated bisphenol (III) is too low, the resulting epoxy resin composition will not have sufficient flame retardancy.

加聚反应可在通用环氧树脂和/或环氧化卤代双酚存在下完成,环氧化卤代双酚是将上述卤代双酚(Ⅲ)与表卤代醇或甲基表卤代醇进行缩水甘油基醚化反应而制备的。当加聚反应是在环氧化卤代双酚存在下进行时。该双酚所用比例优选为每100%(重量)全部含量的1-15%以防止加热时层压制品着色。The polyaddition reaction can be completed in the presence of general-purpose epoxy resins and/or epoxidized halogenated bisphenols. The epoxidized halogenated bisphenols are obtained by combining the above-mentioned halogenated bisphenols (Ⅲ) with epihalohydrin or methyl epihalide It is prepared by glycidyl etherification reaction of substituted alcohol. When the polyaddition reaction is carried out in the presence of epoxidized halogenated bisphenols. The bisphenol is preferably used in a proportion of 1-15% per 100% by weight of the total content to prevent coloring of the laminate when heated.

主要含有由环氧树脂(A)和卤代双酚(Ⅲ)如上所述反应制成的加聚合物树脂(B)的本发明环氧树脂组合物具有300-500克/当量的环氧当量,其数均分子量Mn为500-1000,Mn/Mw比值为1.7-3.0,卤化物含量为15-25%(重量),和多官能组分含量为3-40%(重量)。它是一种粘滞产品,具有窄分子量分布,含有少量低和高分子量物质。The epoxy resin composition of the present invention mainly comprising the polymer-added resin (B) prepared by the reaction of the epoxy resin (A) and the halogenated bisphenol (III) as described above has an epoxy equivalent of 300-500 g/equivalent , the number average molecular weight Mn is 500-1000, the Mn/Mw ratio is 1.7-3.0, the halide content is 15-25% (weight), and the multifunctional component content is 3-40% (weight). It is a viscous product with a narrow molecular weight distribution containing small amounts of low and high molecular weight species.

主要含有加聚合物树脂(D)(该树脂由环氧树脂(C)与卤代双酚(Ⅲ)如上所述反应而制成)的本发明环氧树脂组合物具有300-500克/当量的环氧当量,数均分子量Mn为500-1000,Mn/Mw比值为1.5-2.5,卤代物含量为15-25%(重量)。以及多官能组分含量为3-40%重量。它是一种粘滞产品,具有窄分子量分布,含有少量低和高分子量物质。The epoxy resin composition of the present invention mainly containing the polymer-added resin (D) which is prepared by reacting the epoxy resin (C) with the halogenated bisphenol (III) as described above) has 300-500 g/equivalent The epoxy equivalent, the number average molecular weight Mn is 500-1000, the Mn/Mw ratio is 1.5-2.5, and the halogenated content is 15-25% (weight). And the multifunctional component content is 3-40% by weight. It is a viscous product with a narrow molecular weight distribution containing small amounts of low and high molecular weight species.

当本发明的环氧树脂组合物用例如双氰胺这样的固化剂或酚式novolak树脂进行固化时,所得固化的产物具有改进的耐起泡性。并且比用本发明环氧树脂(A)或(C)以外的其它常规环氧树脂制备的环氧树脂固化制品的玻璃化温度Tg高大约10℃。本发明的环氧树脂组合物还呈现对玻璃布良好的浸渍性。When the epoxy resin composition of the present invention is cured with a curing agent such as dicyandiamide or a phenolic novolak resin, the resulting cured product has improved resistance to blistering. And it is about 10°C higher than the glass transition temperature Tg of epoxy resin cured articles prepared with other conventional epoxy resins other than the epoxy resin (A) or (C) of the present invention. The epoxy resin composition of the present invention also exhibits good impregnation properties for glass cloth.

如上所述,将缩水甘油基醚化的环氧树脂(A)或(C)用来制备本发明的环氧树脂组合物。在本发明环氧树脂组合物的制备中,环氧树脂(A)或(C)可单独使用或与另一种在一个分子中有两个或多个环氧基的环氧树脂结合使用。此附加的环氧树脂的示范例包括双酚-A环氧树脂,酚novolak环氧树脂,甲酚novolak环氧树脂和其它缩水甘油基醚化的环氧树脂,缩水甘油酯环氧树脂,缩水甘油胺环氧树脂,线性脂族环氧树脂,脂环族环氧树脂,杂环环氧树脂,卤代环氧树脂,以及其它多官能环氧树脂,此附加环氧树脂的用量为每100%(重量)总环氧含量(即,环氧树脂和附加环氧树脂的全部)的高达50%(重量),当附加环氧树脂使用过量时,所得组合物就不再具有本发明组合物的性能特点。As mentioned above, the glycidyl etherified epoxy resin (A) or (C) is used to prepare the epoxy resin composition of the present invention. In the preparation of the epoxy resin composition of the present invention, the epoxy resin (A) or (C) may be used alone or in combination with another epoxy resin having two or more epoxy groups in one molecule. Examples of such additional epoxy resins include bisphenol-A epoxy resins, phenol novolak epoxy resins, cresol novolak epoxy resins and other glycidyl etherified epoxy resins, glycidyl ester epoxy resins, shrink Glycerylamine epoxy resins, linear aliphatic epoxy resins, cycloaliphatic epoxy resins, heterocyclic epoxy resins, halogenated epoxy resins, and other multifunctional epoxy resins, the amount of this additional epoxy resin is per 100 % (weight) up to 50% (weight) of the total epoxy content (i.e., the total of epoxy resin and additional epoxy resin), when the additional epoxy resin is used in excess, the resulting composition no longer has the composition of the present invention performance characteristics.

与本发明环氧树脂组合物结合使用的固化剂并不限于任何特定的类型。代表性的固化剂是酸酐,芳族多胺,脂族多胺,咪唑,及酚树脂。The curing agents used in conjunction with the epoxy resin compositions of the present invention are not limited to any particular type. Representative curing agents are acid anhydrides, aromatic polyamines, aliphatic polyamines, imidazoles, and phenolic resins.

示范性的酸酐包括邻苯二甲酸酐,六氢化邻苯二甲酸酐,甲基四氢化邻苯二甲酸酐,甲基六氢化邻苯二甲酸酐,methylnadic酐,甲基萘二羧酸,1,2,4,5-苯四酸酐,1,2,4-苯三酸酐,二苯酮四羧酸酐,十二烷基琥珀酸酐,氯菌酸酐,和氯降冰片烯二羧酸酐。Exemplary anhydrides include phthalic anhydride, hexahydrophthalic anhydride, methyltetrahydrophthalic anhydride, methylhexahydrophthalic anhydride, methylnadic anhydride, methylnaphthalene dicarboxylic acid, 1 , 2,4,5-Pellimetic anhydride, 1,2,4-Pellimetic anhydride, Benzophenone tetracarboxylic anhydride, Dodecylsuccinic anhydride, Chlorendramide, and Chlornorbornene dicarboxylic anhydride.

示范性芳族多胺包括二氨基二苯甲烷,二氨基二苯基砜,和胺加合物。Exemplary aromatic polyamines include diaminodiphenylmethane, diaminodiphenylsulfone, and amine adducts.

示范性脂族多胺包括三亚乙基四胺,二亚乙基三胺,

Figure 94103299X_IMG4
烯二胺,N-氨基乙基哌啶,异佛尔酮二胺,3,9-双(3-氨基丙基)-2,4,8,10-四螺[5.5]十一烷,胺加合物。Exemplary aliphatic polyamines include triethylenetetramine, diethylenetriamine,
Figure 94103299X_IMG4
Diamine, N-aminoethylpiperidine, isophoronediamine, 3,9-bis(3-aminopropyl)-2,4,8,10-tetraspiro[5.5]undecane, amine adduct.

示范性咪唑包括2-甲基咪唑,2-乙基-4-甲基咪唑,2-苯基咪唑,2-十一烷基咪唑,2-乙基-4-甲基咪唑吖嗪,和1-苄基-2-甲基咪唑。Exemplary imidazoles include 2-methylimidazole, 2-ethyl-4-methylimidazole, 2-phenylimidazole, 2-undecylimidazole, 2-ethyl-4-methylimidazolazine, and 1 -Benzyl-2-methylimidazole.

示范性酚树脂包括酚novolak树脂和烷基取代的酚novolak树脂。Exemplary phenolic resins include phenolic novolak resins and alkyl-substituted phenolic novolak resins.

在本发明中也可使用如双氰胺(dicyanediamide),m-亚二甲苯基二胺选择的固化剂。Optional curing agents such as dicyanediamide, m-xylylenediamine can also be used in the present invention.

在本发明中,如上所说的固化剂既可单独使用,也可以两或多个结合使用。In the present invention, the above-mentioned curing agents can be used alone or in combination of two or more.

固化剂可与固化促进剂一起使用。示范性固化促进剂包括如上所述的咪唑,例如,1-苄基-2-甲基咪唑和2-乙基-4-甲基咪唑,诸如叔胺之类的胺,例如N,N-苄基二甲胺和2,4,6-三(二甲基氨甲基)酚;和叔膦如三苯基膦。Curing agents can be used together with curing accelerators. Exemplary curing accelerators include imidazoles as described above, for example, 1-benzyl-2-methylimidazole and 2-ethyl-4-methylimidazole, amines such as tertiary amines, such as N,N-benzyl dimethylamine and 2,4,6-tris(dimethylaminomethyl)phenol; and tertiary phosphines such as triphenylphosphine.

其它示范性固化促进剂是1,8-二氮双环-[5.4.0]-十一碳烯-7辛酸酯,单乙胺和三氟化硼的配合物,和可从Sun  Abbot  Inc买到的商品名为Ucat  SA102的化合物。Other exemplary curing accelerators are 1,8-diazabicyclo-[5.4.0]-undecene-7-octanoate, a complex of monoethylamine and boron trifluoride, and ® commercially available from Sun Abbot Inc. The trade name Ucat SA102 compound obtained.

在本发明中,固化促进剂可单独使用或以两个或多个结合使用。In the present invention, the curing accelerators may be used alone or in combination of two or more.

本发明的环氧树脂组合物可与一种溶剂进行混合,该溶剂为例如丙酮,甲乙酮,甲苯,二甲苯,甲基异丁酮,醋酸乙酯,乙二醇单甲醚,N,N-二甲基甲酰胺,N,N-二甲基乙酰胺,甲醇,乙醇,等。它们可以单独使用或以两个或多个结合作为混合溶剂使用。The epoxy resin composition of the present invention can be mixed with a solvent such as acetone, methyl ethyl ketone, toluene, xylene, methyl isobutyl ketone, ethyl acetate, ethylene glycol monomethyl ether, N, N- Dimethylformamide, N,N-dimethylacetamide, methanol, ethanol, etc. They may be used alone or in combination of two or more as a mixed solvent.

本发明的环氧树脂组合物依据该组合物预期用途可含有或不含有其它添加剂例如阻燃剂和填料。The epoxy resin composition of the present invention may or may not contain other additives such as flame retardants and fillers depending on the intended use of the composition.

本发明的环氧树脂组合物完全合适根据常规方法制备铜包层环氧树脂层压制品,在典型的制备铜包层环氧树脂层压制品中使用本发明的环氧树脂组合物,首先将环氧树脂溶于一种溶剂中制备一种漆,然后用这样制备的漆浸渍和/或施加于玻璃布这样的补强材料并在高温干燥除去溶剂制出预浸料坯。下一步,在预浸料坯的一或两个表面配置铜包层,预浸料坯以单片使用或以预浸料坯片的叠片使用,环氧树脂组合物允许根据常规方法通过加热和施压而固化。The epoxy resin composition of the present invention is fully suitable for preparing copper-clad epoxy resin laminates according to conventional methods. In a typical preparation of copper-clad epoxy resin laminates, the epoxy resin composition of the present invention is used. Epoxy resin is dissolved in a solvent to prepare a varnish, which is then impregnated and/or applied to a reinforcing material such as glass cloth and dried at high temperature to remove the solvent to produce a prepreg. In the next step, a copper clad layer is provided on one or both surfaces of the prepreg. The prepreg is used as a single sheet or as a stack of prepreg sheets. The epoxy resin composition is allowed to and solidify under pressure.

通过以下的实例和对比例进一步详述本发明。应注意该实例并不意味着限定本发明范围。The present invention is further described in detail by the following examples and comparative examples. It should be noted that this example is not meant to limit the scope of the invention.

实例example

在以下的实例和对比例中,粘度,挠曲强度,挠曲模量和负载下的挠曲温度均按如下所述进行评价。In the following examples and comparative examples, viscosity, flexural strength, flexural modulus and deflection temperature under load were evaluated as follows.

粘度viscosity

粘度在25℃温度用E-型粘度计测量。The viscosity was measured with an E-type viscometer at a temperature of 25°C.

挠曲强度和挠曲模量Flexural strength and flexural modulus

将尺寸为4毫米×10毫米×97毫米的样品根据JIS  K6911使用TOYO  BALDWIN制造的Tensilon以1毫米/分的滑动横梁速度用最大500公斤负荷的传感器进行测定。A sample with a size of 4 mm x 10 mm x 97 mm was measured in accordance with JIS K6911 using a Tensilon manufactured by TOYO BALDWIN at a sliding beam speed of 1 mm/min with a sensor with a maximum load of 500 kg.

负载下的挠曲温度Deflection temperature under load

将尺寸为12.5毫米×12.5毫米×125毫米的样品根据JIS  K6911使用Tester  Industry  K.K制造的装置测定。A sample having a size of 12.5 mm×12.5 mm×125 mm was measured according to JIS K6911 using an apparatus manufactured by Tester Industry K.K.

合成例1Synthesis Example 1

用双酚A作为酚合成novolak树脂Synthesis of novolak resin with bisphenol A as phenol

在装有冷凝器,温度计,搅拌器和滴落容器的1升可分离烧瓶中加入456克双酚A和335克甲苯,然后将内容物在搅拌下加热。当烧瓶内温度达到70℃时,加入2.52克作为催化剂的草酸二水合物。当烧瓶内温度达到90℃时,用2小时滴加37%的甲醛水溶液82.7克。在回流条件下将内容物再搅拌1小时。内容物的温度被进一步升高因而从该系统中除去水和甲苯。当温度达到150℃时,将内容物在常温下浓缩1小时,在20mmHg的减压下进一步浓缩1小时得到一种双酚A  novolak树脂(以下称作novolak树脂(Ⅰ))。用Metler  Inc生产的自动软化点测量装置测定该novolak树脂(Ⅰ)的软化点为93℃。根据JISK0070也测定了该novolak树脂的羟基当量,为120克/当量。其数均分子量为450,分子量分布1.50。Into a 1 liter separable flask equipped with a condenser, thermometer, stirrer and dropping vessel were charged 456 grams of bisphenol A and 335 grams of toluene and the contents were heated with stirring. When the temperature in the flask reached 70°C, 2.52 g of oxalic acid dihydrate was added as a catalyst. When the temperature in the flask reached 90°C, 82.7 grams of 37% formaldehyde solution was added dropwise in 2 hours. The contents were stirred at reflux for an additional 1 hour. The temperature of the contents is raised further thereby removing water and toluene from the system. When the temperature reached 150°C, the contents were concentrated at normal temperature for 1 hour, and further concentrated for 1 hour under a reduced pressure of 20 mmHg to obtain a bisphenol A novolak resin (hereinafter referred to as novolak resin (I)). The softening point of this novolak resin (I) was measured to be 93°C with an automatic softening point measuring device manufactured by Metler Inc. The hydroxyl equivalent of this novolak resin was also measured according to JIS K0070, and it was 120 g/equivalent. Its number average molecular weight was 450, and its molecular weight distribution was 1.50.

例1example 1

在装有搅拌器,回流冷凝器,滴液漏斗,和温度计的反应器中加入400克双酚A,100克邻-甲酚novolak树脂(由Nippon  Kayaku  K.K制造的OCN80;软化点为80℃,羟基当量139克/当量,数均分子量为425,分子量分布为1.30),1956克表氯代醇,和39克水。将内容物的温度升至65℃。当反应混合物成为均匀溶液时,加入23.1克50%氯化四甲铵水溶液并在搅拌下让反应进行3小时。Add 400 grams of bisphenol A, 100 grams of o-cresol novolak resin (OCN80 manufactured by Nippon Kayaku K.K; softening point is 80 ℃, Hydroxyl equivalent weight 139 g/eq, number average molecular weight 425, molecular weight distribution 1.30), 1956 g epichlorohydrin, and 39 g water. The temperature of the contents was raised to 65°C. When the reaction mixture became a homogeneous solution, 23.1 g of a 50% aqueous solution of tetramethylammonium chloride was added and the reaction was allowed to proceed for 3 hours with stirring.

下一步用2小时在70℃减压下将331.5克48%NaOH水溶液滴加到混合物中,并利用表氯代醇和水的共沸从系统中除去过量的水,使反应系统中保持2%(重量)的水含量。与水蒸馏出的表氯代醇与水分离再循环于该反应系统。共沸蒸馏的条件(包括减压及加热的程度)要控制每单位时间从系统中除去的水量应等于加到反应系统中的48%NaOH水溶液中的水量和反应中所生成的水量的总和。滴加48%NaOH水溶液完成之后,将该反应系统保持在相同的温度再搅拌0.5小时。In the next step, 331.5 grams of 48% NaOH aqueous solution was added dropwise to the mixture under reduced pressure at 70 °C for 2 hours, and the excess water was removed from the system by azeotroping of epichlorohydrin and water, so that the reaction system remained at 2% ( weight) of water content. The epichlorohydrin distilled off from water is separated from water and recycled to the reaction system. The conditions of azeotropic distillation (including the degree of decompression and heating) should be controlled so that the amount of water removed from the system per unit time should be equal to the sum of the amount of water in the 48% NaOH aqueous solution added to the reaction system and the amount of water generated in the reaction. After the dropwise addition of 48% NaOH aqueous solution was completed, the reaction system was kept at the same temperature and stirred for another 0.5 hours.

反应完成后,在减压下从反应混合物中蒸馏出表氯代醇和水。在残留的混合物内加入750克二甲苯和75克水。将该反应混合物在80℃搅拌0.5小时,并让其静止分成二甲苯和水相。从二甲苯相收集的样品分析呈现1.45%(重量)的可水解氯浓度。After the reaction was completed, epichlorohydrin and water were distilled off from the reaction mixture under reduced pressure. To the remaining mixture were added 750 grams of xylene and 75 grams of water. The reaction mixture was stirred at 80°C for 0.5 hours and allowed to stand to separate into xylene and aqueous phases. Analysis of a sample collected from the xylene phase showed a hydrolyzable chlorine concentration of 1.45% by weight.

下一步,在二甲苯相中加入62克48%的NaOH水溶液并将反应混合物在95℃搅拌2小时。反应完成后,除去凝胶含量,为了中和加入750克25%磷酸单钠水溶液。通过利用二甲苯-水的共沸从所得中和的产物中除去水,将残留的混合物用玻璃过滤器过滤分离出中和产品中的无机盐。将此滤液在减压下加热至150℃除去二甲苯得到680克环氧树脂。这样生产的环氧树脂具有185克/当量的环氧当量和0.06%(重量)的可水解氯含量。Next, 62 g of a 48% aqueous NaOH solution were added to the xylene phase and the reaction mixture was stirred at 95°C for 2 hours. After the reaction was complete, the gel content was removed, and 750 grams of 25% monosodium phosphate aqueous solution was added for neutralization. Water was removed from the resulting neutralized product by using xylene-water azeotropy, and the remaining mixture was filtered with a glass filter to separate inorganic salts in the neutralized product. The filtrate was heated to 150°C under reduced pressure to remove xylene to obtain 680 g of epoxy resin. The epoxy resin thus produced had an epoxy equivalent of 185 g/eq and a hydrolyzable chlorine content of 0.06% by weight.

例2Example 2

重复例1的程序不同是所用双酚A的量减小至260克,所用邻-甲酚novolak树脂被参考合成例1中合成的novolak树脂(Ⅰ)代替。生产出450克环氧树脂,其环氧当量为190克/当量而可水解氯含量为0.05%(重量)。The difference of repeating the procedure of Example 1 is that the amount of bisphenol A used is reduced to 260 grams, and the o-cresol novolak resin used is replaced by the novolak resin (I) synthesized in the reference synthesis example 1. 450 g of epoxy resin having an epoxy equivalent weight of 190 g/equivalent and a hydrolyzable chlorine content of 0.05% by weight were produced.

例3Example 3

将例1合成的80克环氧树脂,72.6克甲基六氢化邻苯二甲酸酐(由Shin-Nippon  Rika  K.K生产的Liquacid  MH-700),和0.4克1,8-二氮杂双环[5.4.0]-7-十一碳烯Octilate(由Sun-Abbot  Inc生产,Ucat-102)在50℃搅拌下混合制成均匀的漆溶液。此均匀的溶液在25℃具有993厘泊的粘度。80 g of epoxy resin synthesized in Example 1, 72.6 g of methylhexahydrophthalic anhydride (Liquacid MH-700 produced by Shin-Nippon Rika K.K), and 0.4 g of 1,8-diazabicyclo[5.4 .0]-7-Undecene Octilate (manufactured by Sun-Abbot Inc, Ucat-102) was mixed under stirring at 50°C to make a homogeneous paint solution. This homogeneous solution has a viscosity of 993 centipoise at 25°C.

把这样生产的均匀溶液倒入为制备测量挠曲强度和挠曲模量的测试样品而配置的模具内,另外还倒入为载荷下测量挠曲温度的测试样品而配置的模具内,然后在120℃加热2小时,在150℃加热2小时,最后在170℃加热4小时进行固化。将这样固化的测试样品分别测定其挠曲强度,挠曲模量和载荷下的挠曲温度。结果示于表1。The homogeneous solution thus produced was poured into molds prepared for preparing test samples for measuring flexural strength and flexural modulus, and additionally poured into molds prepared for test samples for measuring deflection temperature under load, and then placed in Heating at 120°C for 2 hours, heating at 150°C for 2 hours, and finally heating at 170°C for 4 hours for curing. The test specimens thus cured were measured for their flexural strength, flexural modulus and deflection temperature under load, respectively. The results are shown in Table 1.

例4Example 4

重复例3的程序,不同是所用的环氧树脂用80克例2合成的环氧树脂代替,所用的甲基六氢邻苯二甲酸酐的用量被减少到70.8克。所得均匀溶液具有896厘泊的粘度(在25℃)。该均匀溶液也被固化成测试样品以测定其挠曲强度、挠曲模量和载荷下挠曲温度。结果示于表1。The procedure of Example 3 was repeated, except that the epoxy resin used was replaced by 80 grams of epoxy resin synthesized in Example 2, and the amount of methylhexahydrophthalic anhydride used was reduced to 70.8 grams. The resulting homogeneous solution had a viscosity (at 25°C) of 896 centipoise. This homogeneous solution was also cured into test specimens to determine their flexural strength, flexural modulus, and deflection temperature under load. The results are shown in Table 1.

对比例1Comparative example 1

重复例1的程序,不同是没有使用双酚-A而仅用邻-甲酚novolak树脂(由Nippon  Kayaku  K.K制造的OCN80)584克来生产650克novolak环氧树脂。这样生产的novolak环氧树脂具有203克/当量的环氧当量和0.05%(重量)的可水解氯含量。The procedure of Example 1 was repeated except that no bisphenol-A was used and only 584 g of o-cresol novolak resin (OCN80 manufactured by Nippon Kayaku K.K) was used to produce 650 g of novolak epoxy resin. The novolak epoxy resin thus produced had an epoxy equivalent of 203 g/eq and a hydrolyzable chlorine content of 0.05% by weight.

对比例2Comparative example 2

重复例1的程序,不同是没有使用双酚-A而将邻-甲酚novolak树脂用参考合成例1中合成的双酚Anovolak树脂504克来代替制成605克novolak环氧树脂,这样制成的novolak环氧树脂具有197克/当量的环氧当量和0.06%(重量)的可水解氯含量。Repeat the procedure of Example 1, the difference is that no bisphenol-A is used and the o-cresol novolak resin is replaced with 504 grams of bisphenol Anovolak resin synthesized in reference synthesis example 1 to make 605 grams of novolak epoxy resin, which is made The novolak epoxy resin has an epoxy equivalent weight of 197 g/eq and a hydrolyzable chlorine content of 0.06% by weight.

对比例3Comparative example 3

重复例3的程序,不同是用16克对比例1合成的novolak环氧树脂,64克双酚A型液体环氧树脂(环氧当量,188克/当量),71.4克甲基六氢邻苯二甲酸酐,和0.4克1,8-二氮杂双环[5.4.0]-7-十一碳烯Octilate(由Sun-Abbot  Inc生产的Ucat-102)制备一种均匀的漆溶液。该均匀溶液在25℃的粘度为1946厘泊。把这样制成的均匀溶液固化为测试样品以测量挠曲强度、挠曲模量和载荷下挠曲温度。在固化产品中双酚A组分对novolak组分之比和例3相同。结果示于表1。Repeat the procedure of example 3, the difference is the novolak epoxy resin synthesized with 16 grams of comparative example 1, 64 grams of bisphenol A type liquid epoxy resin (epoxy equivalent, 188 grams/equivalent), 71.4 grams of methylhexahydro-phthalate Diformic anhydride, and 0.4 g of 1,8-diazabicyclo[5.4.0]-7-undecene Octilate (Ucat-102, manufactured by Sun-Abbot Inc.) prepare a uniform paint solution. The homogeneous solution had a viscosity of 1946 centipoise at 25°C. The homogeneous solution thus prepared was cured as a test sample to measure flexural strength, flexural modulus and deflection temperature under load. The ratio of the bisphenol A component to the novolak component in the cured product was the same as in Example 3. The results are shown in Table 1.

对比例4Comparative example 4

重复例3的程序,不同是用37.4克对比例2合成的novolak环氧树脂,42.6克双酚A型液体环氧树脂(环氧当量:188克/当量)69.8克甲基六氢邻苯二甲酸酐,和0.4克1,8-二氮杂双环[5.4.0]-7-十一碳烯Octilate(由Sun-Abbot  Inc生产的Ucat-102)制备一种均匀的漆溶液。该均匀溶液在25℃的粘度为3379厘泊。将这样制备的均匀溶液固化为测试样品以测量挠曲强度、挠曲模量和载荷下挠曲温度。固化产品中双酚A组分对novolak组分之比与例4相同,结果示于表1。Repeat the procedure of example 3, the difference is to use the novolak epoxy resin synthesized by 37.4 grams of comparative example 2, 42.6 grams of bisphenol A type liquid epoxy resin (epoxy equivalent: 188 grams/equivalent) 69.8 grams of methylhexahydrophthalate Formic anhydride, and 0.4 g of 1,8-diazabicyclo[5.4.0]-7-undecene Octilate (Ucat-102 from Sun-Abbot Inc.) were used to prepare a uniform paint solution. The homogeneous solution had a viscosity of 3379 centipoise at 25°C. The homogeneous solution thus prepared was cured as a test sample to measure flexural strength, flexural modulus, and deflection temperature under load. The ratio of the bisphenol A component to the novolak component in the cured product is the same as in Example 4, and the results are shown in Table 1.

对比例5Comparative example 5

重复例3的程序,不同是用80克双酚A型液体环氧树脂(环氧当量188克/当量),71.5克甲基六氢邻苯二甲酸酐和0.4克Ucat-102制备一均匀漆溶液。将这样制成的均匀溶液固化为测试样品以测量其挠曲强度、挠曲模量和载荷下挠曲温度。结果示于表1。Repeat the procedure of Example 3, the difference is to prepare a uniform paint with 80 grams of bisphenol A type liquid epoxy resin (epoxy equivalent 188 grams/equivalent), 71.5 grams of methyl hexahydrophthalic anhydride and 0.4 grams of Ucat-102 solution. The homogeneous solution thus prepared was cured as a test sample to measure its flexural strength, flexural modulus, and deflection temperature under load. The results are shown in Table 1.

表1:固化产品的性质Table 1: Properties of Cured Products

例3  例4  对比例3  对比例4  对比例5Example 3 Example 4 Comparative Example 3 Comparative Example 4 Comparative Example 5

固化前漆在25℃  993  896  1946  3379  -Paint before curing at 25°C 993 896 1946 3379 -

的粘度,厘泊Viscosity, centipoise

挠曲强度,公斤/  12.9  12.9  12.0  12.1  11.8Flexural strength, kg/ 12.9 12.9 12.0 12.1 11.8

毫米2 mm2

挠曲模量,公斤/  279  292  280  280  277Flexural modulus, kg/ 279 292 280 280 277

毫米2 mm2

载荷下挠曲温度,  159  164  160  165  140Deflection temperature under load, 159 164 160 165 140

合成例2至5Synthesis Examples 2 to 5

novolak树脂的合成Synthesis of novolak resin

在装有冷凝器、温度计、搅拌器和滴落容器的1升可分离烧瓶中加入456克双酚A和335克甲苯,将内容物搅拌加热。当烧瓶内温度达到70℃时,加入作为催化剂的2.52克草酸二水合物。当烧瓶内温度达到90℃时,用2小时滴加130克37%甲醛水溶液,在回流和搅拌条件下让该反应再进行1小时。下一步,将系统温度升高从系统中除去水和甲苯。当温度达到150℃时,在常温度下将内容物浓缩1小时,在20mmHg减压下进一步浓缩1小时,得到含有残留双酚A的novolak环氧树脂,以下将其称为novolak树脂(2)。用Metler  Inc生产的自动软化点测量装置测定所得novolak树脂(2)的软化点。还用凝胶渗透色谱法(GPC)测定该树脂的双酚A单体残留含量以及数均分子量和分子量分布(Mw/Mn)。在双酚A单体残留含量的测定中,2柱Shim-Pack-HSG-10(由Shimadzu  Seisakusho  Ltd制造)和每1柱Shim-Pack-HSG15和20串联连接构成分离柱。在分子量的测定中,将HSG-20、40、50和60串联连接。将四氢呋喃用作洗脱溶液。分子量分布按以下所述进行测量。结果示于表2。Into a 1 liter separable flask equipped with a condenser, thermometer, stirrer and dropping vessel was charged 456 grams of bisphenol A and 335 grams of toluene and the contents were stirred and heated. When the temperature in the flask reached 70°C, 2.52 g of oxalic acid dihydrate was added as a catalyst. When the temperature in the flask reached 90°C, 130 g of a 37% aqueous formaldehyde solution was added dropwise over 2 hours, and the reaction was allowed to proceed for another 1 hour under reflux and stirring. Next, the temperature of the system was raised to remove water and toluene from the system. When the temperature reaches 150°C, concentrate the contents at normal temperature for 1 hour, and further concentrate for 1 hour under reduced pressure of 20 mmHg to obtain novolak epoxy resin containing residual bisphenol A, which is hereinafter referred to as novolak resin (2) . The softening point of the obtained novolak resin (2) was measured with an automatic softening point measuring device manufactured by Metler Inc. The residual bisphenol A monomer content as well as the number average molecular weight and molecular weight distribution (Mw/Mn) of the resin were also determined by gel permeation chromatography (GPC). In the measurement of the bisphenol A monomer residual content, 2 columns Shim-Pack-HSG-10 (manufactured by Shimadzu Seisakusho Ltd) and each 1 column Shim-Pack-HSG15 and 20 were connected in series to constitute a separation column. In the determination of molecular weight, HSG-20, 40, 50 and 60 were connected in series. Tetrahydrofuran was used as the eluting solution. The molecular weight distribution was measured as described below. The results are shown in Table 2.

重复以上所述参考合成例2的程序,不同是双酚A、草酸二水合物,和37%甲醛水溶液的用量如表2所示从而制成novolak树脂(3)至(5)。这样得到的novolak树脂(3)-(5)也测定其软化点,双酚A单体残留含量,数均分子量,和分子量分布。注意合成例5的情况是使用324克邻-甲酚代替双酚A。Repeat the above-mentioned procedure of Reference Synthesis Example 2, except that the amounts of bisphenol A, oxalic acid dihydrate, and 37% formaldehyde solution are as shown in Table 2 to prepare novolak resins (3) to (5). The novolak resins (3)-(5) thus obtained were also measured for their softening point, residual bisphenol A monomer content, number average molecular weight, and molecular weight distribution. Note that in the case of Synthesis Example 5, 324 g of o-cresol was used instead of bisphenol A.

表2:Table 2:

novolak  树脂novolak resin

(2)  (3)  (4)  (5)(2) (3) (4) (5)

加入原料的重量,克Added raw material weight, grams

双酚-A  456  456  456  -Bisphenol-A 456 456 456 -

邻-甲酚  -  -  -  324o-Cresol - - - 324

草酸二水合物  2.52  2.52  2.52  3.8Oxalic acid dihydrate 2.52 2.52 2.52 3.8

37%甲醛水溶液  130  82.7  33.1  17437% formaldehyde solution 130 82.7 33.1 174

所得产品的性质The nature of the resulting product

软化点,℃  110  93  72  80Softening point, ℃ 110 93 72 80

残留双酚-A单体 22 39 57 23* Residual bisphenol-A monomer 22 39 57 23 *

含量,%(重量)Content,%(weight)

数均分子量  556  450  374  425Number average molecular weight 556 450 374 425

分子量分布(Mw/Mn)  1.68  1.50  1.12  1.30Molecular weight distribution (Mw/Mn) 1.68 1.50 1.12 1.30

注:*  为双核形式邻-甲酚的含量Note: * is the content of dinuclear o-cresol

合成例6至15Synthesis Examples 6 to 15

缩水甘油基醚化的环氧树脂的合成(共缩水甘油基化)Synthesis of Glycidyl Etherified Epoxy Resins (Coglycidylation)

在装有温度计、搅拌器、分离器、冷凝器和滴落容器的2升圆底烧瓶中加入200克具有22%(重量)残留双酚-A单体含量的novolak树脂(2)和1206克表氯代醇,在搅拌下将内容物加热至90℃温度。在90℃温度加入30克水和3克氯化四甲铵然后将该混合物搅拌4小时。将该混合物的温度降至70℃,压力降至500mmHg,在此压力下,用3小时从滴落容器向该混合物加入137克48%的氢氧化钠水溶液,同时用分离器从该系统中除去水。完成滴加氢氧化钠之后再继续除去水30分钟。将系统压力降至20mmHg,将该混合物在120℃缩合1小时。然后将压力恢复至常压,向该混合物中加入350克水和250克甲苯,将所得混合物在90℃搅拌30分钟。让该混合物静止从而促进分离,并除去这样分离出的水层,而留下的树脂层在20mmHg和150℃进行浓缩,得到264克缩水甘油基醚化的环氧树脂,以下将其称为环氧树脂(6)。Into a 2 liter round bottom flask equipped with a thermometer, stirrer, separator, condenser and drop vessel were charged 200 g of novolak resin (2) with a residual bisphenol-A monomer content of 22% by weight and 1206 g epichlorohydrin, and heat the contents to a temperature of 90°C with stirring. 30 g of water and 3 g of tetramethylammonium chloride were added at a temperature of 90°C and the mixture was stirred for 4 hours. The temperature of this mixture is reduced to 70 ℃, and the pressure is reduced to 500mmHg, under this pressure, with 3 hours, add 137 grams of 48% sodium hydroxide aqueous solution to this mixture from the drip container, simultaneously remove from this system with separator water. Water removal was continued for an additional 30 minutes after the dropwise addition of sodium hydroxide was complete. The system pressure was lowered to 20 mmHg, and the mixture was condensed at 120°C for 1 hour. Then the pressure was returned to normal pressure, 350 g of water and 250 g of toluene were added to the mixture, and the resulting mixture was stirred at 90° C. for 30 minutes. The mixture was allowed to stand still to facilitate separation, and the thus separated aqueous layer was removed, and the remaining resin layer was concentrated at 20 mmHg and 150° C. to obtain 264 g of glycidyl etherified epoxy resin, hereinafter referred to as cyclo Oxygen Resin (6).

用盐酸二噁烷法对这样制得的环氧树脂(6)测定其环氧当量。还要用Metler  Inc制造的自动软化点测试设备测定环氧树脂(6)的软化点,并像合成例2至5的情况那样用凝胶渗透色谱法(GPC)测定其组成。结果示于表3。The epoxy equivalent of the epoxy resin (6) thus obtained was measured by the dioxane hydrochloride method. Also, the softening point of the epoxy resin (6) was measured using an automatic softening point measuring apparatus manufactured by Metler Inc., and its composition was measured by gel permeation chromatography (GPC) as in the case of Synthesis Examples 2 to 5. The results are shown in Table 3.

重复合成例6的程序,不同是novolak树脂,双酚A,表氯代醇,和48%NaOH水溶液的用量如表3所示,制成环氧树脂(7)至(15)。该所得环氧树脂(7)至(15)也测定其环氧当量,软化点和组成,结果也示于表3。The procedure of Synthesis Example 6 was repeated, except that the amounts of novolak resin, bisphenol A, epichlorohydrin, and 48% NaOH aqueous solution were as shown in Table 3 to prepare epoxy resins (7) to (15). The obtained epoxy resins (7) to (15) were also measured for epoxy equivalent, softening point and composition, and the results are also shown in Table 3.

Figure 94103299X_IMG5
Figure 94103299X_IMG5

合成例16-27加聚合物树脂的合成Synthesis Example 16-27 Synthesis of Polymer Resin

在装有搅拌器和温度计的1升可分离烧瓶中加入171克双酚A环氧树脂(环氧当量,188克/当量),29.4克合成例6制备的环氧树脂(6),和94.3克四溴双酚A,将内容物搅拌加热。当温度达到100℃时,加入0.2克氯化四乙铵,在160℃加速该反应5小时得到一加聚树脂,以下称为加聚合物树脂(16)。In a 1-liter separable flask equipped with a stirrer and a thermometer, add 171 grams of bisphenol A epoxy resin (epoxy equivalent, 188 grams/equivalent), 29.4 grams of epoxy resin (6) prepared in Synthesis Example 6, and 94.3 gram tetrabromobisphenol A, and heat the contents with stirring. When the temperature reached 100°C, 0.2 g of tetraethylammonium chloride was added, and the reaction was accelerated at 160°C for 5 hours to obtain a monoaddition polymer resin, hereinafter referred to as addition polymer resin (16).

用以上所述方法测定该加聚合物树脂(16)的环氧当量。该树脂并通过凝胶渗透色谱法(GPC)使用串联连接的Shim-pack-HSG20、40、50和60柱测定其数均分子量,并用以上所述相同方法测定其分子量分布。The epoxy equivalent weight of the polymer-added resin (16) was determined by the method described above. The number average molecular weight of the resin was determined by gel permeation chromatography (GPC) using Shim-pack-HSG20, 40, 50 and 60 columns connected in series, and its molecular weight distribution was determined by the same method as described above.

重复合成例16的程序,不同是环氧树脂,双酚A环氧树脂,和四溴双酚A的用量如表4所示制备出加聚合物树脂(17)至(25)。该加聚合物树脂(17)至(25)也测定其环氧当量,数均分子量,和分子量分布。The procedure of Synthesis Example 16 was repeated except that the amounts of epoxy resin, bisphenol A epoxy resin, and tetrabromobisphenol A were as shown in Table 4 to prepare polymer-added resins (17) to (25). The addition polymer resins (17) to (25) were also measured for epoxy equivalent, number average molecular weight, and molecular weight distribution.

再重复合成例16的程序,不同是用表4所示数量的四溴双酚A环氧树脂代替四溴双酚A,且环氧树脂和双酚A环氧树脂的用量如表4所示,制成加聚合物树脂(26)和(27)。对加聚合物树脂(26)和(27)也测定其环氧当量,数均分子量,和分子量分布。Repeat the procedure of synthetic example 16 again, difference is to replace tetrabromobisphenol A with the tetrabromobisphenol A epoxy resin of quantity shown in table 4, and the consumption of epoxy resin and bisphenol A epoxy resin is as shown in table 4 , made into polymer-added resins (26) and (27). The epoxy equivalent weight, number average molecular weight, and molecular weight distribution were also determined for the addition polymer resins (26) and (27).

Figure 94103299X_IMG6
Figure 94103299X_IMG6

例5Example 5

在溶于25克甲·乙酮中的100克加聚合物树脂(20)的溶液中加入溶于20克乙二醇单甲醚中的2.5克双氰胺和0.15克2-乙基-4-甲基咪唑溶液制成一种环氧树脂组合物漆。用这样制成的漆浸渍-玻璃布(由Nitto  Boseki  Co,Ltd制备的WEA-18W105F),然后在140℃的干燥加热炉中干燥6分钟制成一预浸料坯。该预浸料坯具有49%(重量)的环氧树脂组合物含量。评价预浸料坯的外观Add 2.5 grams of dicyandiamide and 0.15 grams of 2-ethyl-4 dissolved in 20 grams of ethylene glycol monomethyl ether to a solution of 100 grams of polymer resin (20) dissolved in 25 grams of methyl ethyl ketone - Methylimidazole solution made into an epoxy resin composition paint. The varnish thus prepared was impregnated with a glass cloth (WEA-18W105F manufactured by Nitto Boseki Co, Ltd), followed by drying in a drying oven at 140°C for 6 minutes to prepare a prepreg. The prepreg had an epoxy resin composition content of 49% by weight. Evaluation of prepreg appearance

将该预浸料坯弄皱收集环氧树脂组合物,把这样收集的环氧树脂组合物放入一适合的模具中以生产1毫米厚的测试样片。将该测试样片放入由Toyobo  Co  Ltd制造的Reolosolid中以便在2℃/分的升温速率下测定该环氧树脂组合物的玻璃化转变温度,Tg。The prepreg was crumpled to collect the epoxy resin composition, and the epoxy resin composition thus collected was placed into a suitable mold to produce a test piece of 1 mm thickness. The test piece was placed in a Reolosolid manufactured by Toyobo Co Ltd to measure the glass transition temperature, Tg, of the epoxy resin composition at a heating rate of 2°C/min.

该预浸料坯还可被制成层压制品,即把四片该预浸料坯堆叠起来,并在170℃和20公斤/厘米2压力下模压该迭层1小时。把该层压制品浸没在121℃温度和2公斤/厘米2的水中以预测定的时间期间,然后浸没在260℃焊浴中20秒,经过加压煮沸测试(PCT)后根据以下标准测定该层压制品的耐焊钎热:The prepreg can also be made into a laminate by stacking four sheets of the prepreg and molding the stack at 170°C and a pressure of 20 kg/ cm² for 1 hour. The laminate was immersed in water at a temperature of 121°C and 2 kg/ cm2 for a predetermined period of time, and then immersed in a solder bath at 260°C for 20 seconds. After the pressure boiling test (PCT), the pressure was determined according to the following standard: Resistance to soldering heat of laminated products:

○:不起泡或脱层,○: no blistering or delamination,

△:少量起泡或轻微脱层,及△: A small amount of foaming or slight delamination, and

X:许多起泡或大量脱层。X: Many blisters or a lot of delamination.

结果示于表5中。The results are shown in Table 5.

例6至12Examples 6 to 12

重复例5的程序,分别用表5所示的加聚合物树脂(21)至(27)代替加聚合物树脂(20)制备漆,然后成预浸料坯。把这样制成的漆和预浸料坯测定其玻璃化转变温度,PCT,及按例5情况浸渍后耐焊钎热。结果示于表5。The procedure of Example 5 was repeated, and the polymer-added resins (21) to (27) shown in Table 5 were used instead of the polymer-added resin (20) to prepare paints and then prepregs. The varnish and prepreg thus made were measured for their glass transition temperature, PCT, and resistance to soldering heat after impregnation according to Example 5. The results are shown in Table 5.

Figure 94103299X_IMG7
Figure 94103299X_IMG7

对比例6至12Comparative Examples 6 to 12

重复例5的程序,不同是按表6所示的量使用如表3所示的环氧树脂(6)至(9)和如表4所示的加聚合物树脂(16)至(19)制备环氧树脂组合物漆。然后成预浸料坯。对这样制得的漆和预浸料坯测定其玻璃化转变温度,PCT之后的耐焊钎热,并且按例5的情况进行浸渍。结果示于表6。The procedure of Example 5 was repeated except that the epoxy resins (6) to (9) as shown in Table 3 and the addition polymer resins (16) to (19) as shown in Table 4 were used in the amounts shown in Table 6 Epoxy resin composition paints were prepared. Then into prepreg. The varnishes and prepregs thus produced were determined for their glass transition temperature, resistance to soldering heat after PCT, and impregnated as in Example 5. The results are shown in Table 6.

Figure 94103299X_IMG8
Figure 94103299X_IMG8

合成例28至37Synthesis Examples 28 to 37

缩水甘油基醚化的环氧树脂的制备(共缩水甘油化)Preparation of Glycidyl Etherified Epoxy Resins (Coglycidylation)

在装有温度计、搅拌器、分离器、冷凝器和滴加容器的2升圆底容器中加入30.7克合成例2中合成的novolak树脂(2),171克双酚A,17.5克四溴双酚A,和1178克表氯代醇,在搅拌下把内容物加热至90℃温度。在90℃温度下加入30克水和3克氯化四甲铵,然后将该混合物搅拌4小时。把混合物的温度降至70℃,压力减至500mmHg,在此压力从滴落容器用3小时向该混合物加入142.5克48%氢氧化钠水溶液,同时用分离器从该系统中除去水。完成滴加氢氧化钠水溶液之后再继续除水30分钟。然后将系统压力减至20mmHg该混合物在120℃缩合1小时。然后把压力恢复至常压,向混合物中加入350克水和250克甲苯,所得混合物在90℃搅拌30分钟。让该混合物静止促进水层并除去分离的水层,把留下的树脂层在150℃和20mmHg浓缩1小时,得到1克缩水甘油基醚化环氧树脂,以下将其称为环氧树脂(28)。Add 30.7 grams of novolak resin (2) synthesized in Synthesis Example 2, 171 grams of bisphenol A, 17.5 grams of tetrabromobis Phenol A, and 1178 grams of epichlorohydrin, the contents were heated to a temperature of 90°C with stirring. 30 g of water and 3 g of tetramethylammonium chloride were added at a temperature of 90°C, and the mixture was stirred for 4 hours. The temperature of the mixture was lowered to 70°C and the pressure was reduced to 500 mmHg, at which pressure 142.5 g of a 48% aqueous sodium hydroxide solution was added to the mixture from a dropping vessel over 3 hours while water was removed from the system by a separator. The water removal was continued for another 30 minutes after the dropwise addition of the aqueous sodium hydroxide solution was completed. The system pressure was then reduced to 20 mmHg and the mixture was condensed at 120°C for 1 hour. Then the pressure was returned to normal pressure, 350 g of water and 250 g of toluene were added to the mixture, and the resulting mixture was stirred at 90°C for 30 minutes. Allow the mixture to stand still to promote the water layer and remove the separated water layer, and the remaining resin layer is concentrated at 150° C. and 20 mmHg for 1 hour to obtain 1 gram of glycidyl etherified epoxy resin, which is hereinafter referred to as epoxy resin ( 28).

用盐酸二噁烷方法测定如此制备的环氧树脂(28)的环氧当量。还要用Metler  Inc生产的自动软化点测量装置测定该环氧树脂(28)的软化点,并如合成例2至5的情况通过凝胶渗透色谱法(GPC)测定其组成。The epoxy equivalent weight of the epoxy resin (28) thus prepared was determined by the dioxane hydrochloride method. Also, the softening point of this epoxy resin (28) was measured with an automatic softening point measuring device produced by Metler Inc., and its composition was measured by gel permeation chromatography (GPC) as in the case of Synthesis Examples 2 to 5.

重复合成例28的程序,不同是按表7所示的量使用novolak树脂,双酚A,四溴双酚A,表氯代醇,和48%的NaOH水溶液制备环氧树脂(29)至(37)。对所得环氧树脂(29)-(37),测定其环氧当量,软化点和组成。结果示于表7。Repeat the procedure of Synthetic Example 28, the difference is to use novolak resin in the amount shown in Table 7, bisphenol A, tetrabromobisphenol A, epichlorohydrin, and 48% NaOH aqueous solution to prepare epoxy resin (29) to ( 37). For the obtained epoxy resins (29)-(37), the epoxy equivalent, softening point and composition were determined. The results are shown in Table 7.

Figure 94103299X_IMG9
Figure 94103299X_IMG9

合成例38-48Synthesis Example 38-48

加聚合物树脂的合成Synthesis of Additive Polymer Resins

在装有搅拌器和温度计的1升可分离烧瓶中加入按合成例28制备的环氧树脂(28)200克和78克四溴双酚A,并把内容物在搅拌下加热。当温度达到100℃时,加入0.2克氯化四乙铵,该反应在160℃加速进行5小时得到一种加聚合物树脂,以下将其称为加聚合物树脂(38)。Into a 1 liter separable flask equipped with a stirrer and a thermometer were charged 200 g of epoxy resin (28) prepared in Synthesis Example 28 and 78 g of tetrabromobisphenol A, and the contents were heated with stirring. When the temperature reached 100°C, 0.2 g of tetraethylammonium chloride was added, and the reaction was accelerated at 160°C for 5 hours to obtain a polymer-added resin, hereinafter referred to as polymer-added resin (38).

像合成例16那样测定这样制备的加聚合物树脂(38)的环氧当量。还要通过凝胶渗透色谱法(GPC)使用串联连接的Shim-pack-HSG20、40、50和60的柱来测定该加聚合物树脂(38)的分子量,以及像例16那样测定其分子量分布。结果示于表8。The epoxy equivalent of the thus prepared polymer-added resin (38) was measured in the same manner as in Synthesis Example 16. The molecular weight of the polymer-added resin (38) was also determined by gel permeation chromatography (GPC) using columns of Shim-pack-HSG20, 40, 50 and 60 connected in series, and its molecular weight distribution was determined as in Example 16 . The results are shown in Table 8.

重复合成例38的程序,不同是按表8所示的量来使用环氧树脂,双酚A环氧树脂及四溴双酚-A来制备加聚合物树脂(39)至(47)。也要测定加聚合物树脂(39)至(47)的环氧当量,数均分子量,和分子量分布。结果示于表8。The procedure of Synthesis Example 38 was repeated, except that epoxy resin, bisphenol A epoxy resin and tetrabromobisphenol-A were used in the amounts shown in Table 8 to prepare the addition polymer resins (39) to (47). The epoxy equivalent weight, number average molecular weight, and molecular weight distribution of the polymer-added resins (39) to (47) were also determined. The results are shown in Table 8.

Figure 94103299X_IMG10
Figure 94103299X_IMG10

例13Example 13

在25克甲·乙酮中的100克加聚合物树脂(45)的溶液中加入2.5克双氰胺和0.15克2-乙基-4-甲基咪唑在20克乙二醇单甲基醚中的溶液制成一种环氧树脂组合物的漆。用如此制成的漆浸渍一种玻璃布(由Nitto  Boseki  Co,Ltd制造的WEA-18W05F),然后在140℃的干燥加热炉中干燥6分钟制成一预浸料坯。该预浸料坯具有49%(重量)的环氧树脂组合物含量。评价该预浸料坯的外观Add 2.5 g of dicyandiamide and 0.15 g of 2-ethyl-4-methylimidazole in 20 g of ethylene glycol monomethyl ether to a solution of 100 g of polymer resin (45) in 25 g of methyl ethyl ketone The solution in is made into a paint of epoxy resin composition. A glass cloth (WEA-18W05F manufactured by Nitto Boseki Co., Ltd.) was impregnated with the varnish thus prepared, followed by drying in a drying oven at 140°C for 6 minutes to prepare a prepreg. The prepreg had an epoxy resin composition content of 49% by weight. Evaluate the appearance of the prepreg

用此预浸料坯按例5至12的情况来测定玻璃化转变温度。还要测定该预浸料坯的浸渍性及压力蒸煮试验后(PCT)的耐焊钎热。结果示于表9。Using this prepreg, the glass transition temperature was determined as in Examples 5 to 12. The impregnability of the prepreg and the resistance to soldering heat after the pressure cooking test (PCT) were also measured. The results are shown in Table 9.

例14和15Examples 14 and 15

重复例13的程序,不同是分别用表9中所示的量以加聚合物树脂(46)和(47)代替加聚合物树脂(45),制备预浸料坯漆,然后成预浸料坯。这样制备的漆和预浸料坯按例13中的情形测定其玻璃化转变温度,(PCT)之后的耐焊钎热和浸渍性。结果也示于表9中。Repeat the procedure of Example 13, the difference is that the amount shown in Table 9 is used to add polymer resin (46) and (47) instead of adding polymer resin (45), to prepare prepreg paint, and then into prepreg Blank. The varnishes and prepregs thus prepared were tested as in Example 13 for glass transition temperature, resistance to soldering heat and impregnation after (PCT). The results are also shown in Table 9.

表9Table 9

例13  例14  例15Example 13 Example 14 Example 15

环氧树脂组合物的组成Composition of epoxy resin composition

加聚合物树脂(45)  100Plus Polymer Resin(45) 100

(46)  100(46) 100

(47)  100(47) 100

双氰胺  2.5  2.5  2.5Dicyandiamide 2.5 2.5 2.5

2-乙基-4-甲基咪唑  0.15  0.15  0.152-Ethyl-4-methylimidazole 0.15 0.15 0.15

固化产品的性质The nature of the cured product

玻璃化转变温度,Tg℃  171  170  162Glass transition temperature, Tg℃ 171 170 162

PCT后的耐焊钎热Resistance to soldering heat after PCT

120分钟  0  0  0120 minutes 0 0 0

150分钟  0  0  △150 minutes 0 0 △

漆对玻璃布的浸渍  良好  良好  良好Impregnation of paint on glass cloth good good good good

对比例13至22Comparative Examples 13 to 22

重复例13的程序,不同是按表10所示的量使用表7中所示的环氧树脂(28)至(30)和表(8)中所示的加聚合物树脂(38)至(44)制取环氧树脂组合物的漆,然后成预浸料坯。这样制取的漆和预浸料坯按例13的情形测定其玻璃化转变温度。PCT后的耐焊钎热和浸渍性,结果示于表10。The procedure of Example 13 was repeated except that the epoxy resins (28) to (30) shown in Table 7 and the addition polymer resins (38) to ( 44) Preparation of varnishes of epoxy resin compositions and subsequent prepregs. The glass transition temperature of the lacquer and prepreg thus prepared was determined as in Example 13. Table 10 shows the results of solder heat resistance and immersion resistance after PCT.

Figure 94103299X_IMG11
Figure 94103299X_IMG11

如以上所列举的,本发明的环氧树脂因其在与固化剂混合时呈现相当低的粘度因此而易于成型。一旦固化后,本发明的环氧树脂呈现极好的耐热性以及高机械强度。因此它特别适用于和各种类型的纤维结合使用以构成塑料复合材料。As listed above, the epoxy resin of the present invention is easy to mold because it exhibits a relatively low viscosity when mixed with a curing agent. Once cured, the epoxy resins of the present invention exhibit excellent heat resistance as well as high mechanical strength. Therefore, it is especially suitable for use in combination with various types of fibers to form plastic composite materials.

本发明的环氧树脂组合物含有作为其主要组分的加聚合物树脂,该加聚合物树脂是由本发明的特殊共缩水甘油基醚化环氧树脂的加聚反应而制备的,该组合物对像玻璃布这样的材料呈现极好的浸渍性,而且一旦固化后,该固化的产品显示出极好的耐热性,耐起泡,和对铜包层的粘合。The epoxy resin composition of the present invention contains as its main component the addition polymer resin prepared by the addition polymerization reaction of the special co-glycidyl etherified epoxy resin of the present invention, the composition Exhibits excellent impregnation to materials such as glass cloth, and once cured, the cured product exhibits excellent heat resistance, resistance to blistering, and adhesion to copper cladding.

Claims (15)

1、一种环氧树脂(A),它由双酚(Ⅰ)和酚醛清漆树脂1, a kind of epoxy resin (A), it is made of bisphenol (I) and novolac resin (Ⅱ)与至少选自表卤代醇和甲基表卤代醇之一进行缩水甘油基醚化反应而制得。(II) It is produced by glycidyl etherification reaction with at least one selected from epihalohydrin and methyl epihalohydrin. 2、根据权利要求1的环氧树脂(A),其中所说的双酚(Ⅰ)和所说的酚醛清漆(Ⅱ)所用重量比为1-95∶99-5。2. The epoxy resin (A) according to claim 1, wherein said bisphenol (I) and said novolak (II) are used in a weight ratio of 1-95:99-5. 3、根据权利要求1的环氧树脂(A),其中所说的双酚(Ⅰ)和所说的酚醛清漆树脂(Ⅱ)所用重量比为50-90∶50-10。3. The epoxy resin (A) according to claim 1, wherein said bisphenol (I) and said novolak resin (II) are used in a weight ratio of 50-90:50-10. 4、根据权利要求1至3的环氧树脂(A),其中所说的酚醛清漆树脂(Ⅱ)具有高达110℃的软化点,其数均分子量为1000至300,分子量分布高达2。4. The epoxy resin (A) according to claims 1 to 3, wherein said novolac resin (II) has a softening point up to 110°C, a number average molecular weight of 1000 to 300 and a molecular weight distribution of up to 2. 5、一种含有加聚合物树脂(B)的环氧树脂组合物,该加聚合物树脂(B)的制备是由双酚(Ⅰ)和酚醛清漆(novolak)树脂(Ⅱ)与至少选自表卤代醇和甲基表卤代醇之一进行缩水甘油基醚化而制成环氧树脂(A);再将所说的环氧树脂(A)与卤化双酚(Ⅲ)进行反应制成加聚合物树脂(B)。5. An epoxy resin composition comprising a polymer-added resin (B) prepared from bisphenol (I) and a novolak resin (II) with at least one selected from the group consisting of Epoxy resin (A) is prepared by glycidyl etherification of one of epihalohydrin and methyl epihalohydrin; then said epoxy resin (A) is reacted with halogenated bisphenol (Ⅲ) to prepare Add polymer resin (B). 6、根据权利要求5的环氧树脂组合物,其中所说的环氧树脂(A)和所说卤代双酚(Ⅲ)之间的反应是在至少有选自环氧树脂(E)和环氧化卤代双酚(F)之一存在下而进行的。6. The epoxy resin composition according to claim 5, wherein the reaction between said epoxy resin (A) and said halogenated bisphenol (III) is at least one selected from the group consisting of epoxy resin (E) and Epoxidation is carried out in the presence of one of the halogenated bisphenols (F). 7、根据权利要求6的环氧树脂组合物,其中所说的环氧化的卤代双酚(F)的用量为1~15%(重量)。7. The epoxy resin composition according to claim 6, wherein said epoxidized halogenated bisphenol (F) is used in an amount of 1 to 15% by weight. 8、一种漆,它含有作为其主要组分的一种溶剂以及根据权利要求5至7中任一项的环氧树脂组合物。8. A varnish containing, as its main components, a solvent and the epoxy resin composition according to any one of claims 5 to 7. 9、一种用根据权利要求8的漆浸渍增强物而制备的层压制品。9. A laminate prepared by impregnating a reinforcement with a lacquer according to claim 8. 10、一种含有加聚合物树脂(D)的环氧树脂组合物,该加聚合物树脂(D)是将双酚(Ⅰ),酚醛清漆树脂(Ⅱ),和卤代双酚(Ⅲ)与至少选自表卤代醇和甲基表卤代醇之一进行缩水甘油基醚化生产一种环氧树脂(C);然后把该环氧树脂(C)与卤代双酚(Ⅲ)反应制成加聚合物树脂(D)而制备。10. An epoxy resin composition comprising a polymer-added resin (D) in which bisphenol (I), novolak resin (II), and halogenated bisphenol (III) Glycidyl etherification with at least one selected from epihalohydrin and methyl epihalohydrin to produce an epoxy resin (C); then reacting the epoxy resin (C) with halogenated bisphenol (Ⅲ) Prepared by adding polymer resin (D). 11、根据权利要求10的环氧树脂组合物,其中所说环氧树脂(C)和所说卤代双酚(Ⅲ)之间的反应是在环氧树脂(E)存在下进行的。11. The epoxy resin composition according to claim 10, wherein the reaction between said epoxy resin (C) and said halogenated bisphenol (III) is carried out in the presence of epoxy resin (E). 12、根据权利要求10或11的环氧树脂组合物,其中所说的酚醛清漆树脂(Ⅱ)是有高达110℃的软化点,数均分子量为1000至300,以及分子量分布为高达2。12. The epoxy resin composition according to claim 10 or 11, wherein said novolak resin (II) has a softening point of up to 110°C, a number average molecular weight of 1000 to 300, and a molecular weight distribution of up to 2. 13、根据权利要求11或12任一项的环氧树脂组合物,其中所说的双酚(Ⅰ),所说的酚醛清漆树脂(Ⅱ)和所说的卤代双酚(Ⅲ)的所用重量比为5-80;94-5∶1-15。13. The epoxy resin composition according to any one of claims 11 or 12, wherein said bisphenol (I), said novolak resin (II) and said halogenated bisphenol (III) are used The weight ratio is 5-80; 94-5: 1-15. 14、一种漆,它含有作为其主要组分的一种溶剂和根据权利要求10至13任一项的环氧树脂组合物。14. A varnish comprising, as its main components, a solvent and the epoxy resin composition according to any one of claims 10 to 13. 15、一种用根据权利要求14的漆浸渍增强物而制备的层压制品。15. A laminate prepared by impregnating reinforcements with a lacquer according to claim 14.
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