JPH0375563B2 - - Google Patents
Info
- Publication number
- JPH0375563B2 JPH0375563B2 JP13158189A JP13158189A JPH0375563B2 JP H0375563 B2 JPH0375563 B2 JP H0375563B2 JP 13158189 A JP13158189 A JP 13158189A JP 13158189 A JP13158189 A JP 13158189A JP H0375563 B2 JPH0375563 B2 JP H0375563B2
- Authority
- JP
- Japan
- Prior art keywords
- groups
- allyl
- polyallylated
- bisphenols
- bisphenol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 229930185605 Bisphenol Natural products 0.000 claims description 25
- VPWNQTHUCYMVMZ-UHFFFAOYSA-N 4,4'-sulfonyldiphenol Chemical class C1=CC(O)=CC=C1S(=O)(=O)C1=CC=C(O)C=C1 VPWNQTHUCYMVMZ-UHFFFAOYSA-N 0.000 claims description 18
- 239000003822 epoxy resin Substances 0.000 claims description 18
- 229920000647 polyepoxide Polymers 0.000 claims description 18
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 claims description 13
- 238000006116 polymerization reaction Methods 0.000 claims description 11
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 claims description 9
- 229920005989 resin Polymers 0.000 claims description 9
- 239000011347 resin Substances 0.000 claims description 9
- 239000007787 solid Substances 0.000 claims description 9
- -1 allyl halide Chemical class 0.000 claims description 7
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 7
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 6
- 229920000642 polymer Polymers 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 3
- 239000003518 caustics Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000007870 radical polymerization initiator Substances 0.000 claims description 2
- 150000007524 organic acids Chemical class 0.000 claims 1
- 125000005843 halogen group Chemical group 0.000 description 12
- 235000013824 polyphenols Nutrition 0.000 description 11
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 10
- 150000004967 organic peroxy acids Chemical class 0.000 description 7
- 238000005406 washing Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- KFSLWBXXFJQRDL-UHFFFAOYSA-N Peracetic acid Chemical compound CC(=O)OO KFSLWBXXFJQRDL-UHFFFAOYSA-N 0.000 description 4
- 229910052736 halogen Inorganic materials 0.000 description 4
- 150000002367 halogens Chemical class 0.000 description 4
- 150000008442 polyphenolic compounds Chemical class 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 238000006735 epoxidation reaction Methods 0.000 description 3
- 125000003700 epoxy group Chemical group 0.000 description 3
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- OSDWBNJEKMUWAV-UHFFFAOYSA-N Allyl chloride Chemical compound ClCC=C OSDWBNJEKMUWAV-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- XYPISWUKQGWYGX-UHFFFAOYSA-N 2,2,2-trifluoroethaneperoxoic acid Chemical compound OOC(=O)C(F)(F)F XYPISWUKQGWYGX-UHFFFAOYSA-N 0.000 description 1
- GLVYLTSKTCWWJR-UHFFFAOYSA-N 2-carbonoperoxoylbenzoic acid Chemical compound OOC(=O)C1=CC=CC=C1C(O)=O GLVYLTSKTCWWJR-UHFFFAOYSA-N 0.000 description 1
- ZNQVEEAIQZEUHB-UHFFFAOYSA-N 2-ethoxyethanol Chemical compound CCOCCO ZNQVEEAIQZEUHB-UHFFFAOYSA-N 0.000 description 1
- YNJSNEKCXVFDKW-UHFFFAOYSA-N 3-(5-amino-1h-indol-3-yl)-2-azaniumylpropanoate Chemical compound C1=C(N)C=C2C(CC(N)C(O)=O)=CNC2=C1 YNJSNEKCXVFDKW-UHFFFAOYSA-N 0.000 description 1
- ATVJXMYDOSMEPO-UHFFFAOYSA-N 3-prop-2-enoxyprop-1-ene Chemical compound C=CCOCC=C ATVJXMYDOSMEPO-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- 238000005821 Claisen rearrangement reaction Methods 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 1
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 150000001350 alkyl halides Chemical class 0.000 description 1
- 238000005937 allylation reaction Methods 0.000 description 1
- 238000012647 allylic polymerization Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- LBAYFEDWGHXMSM-UHFFFAOYSA-N butaneperoxoic acid Chemical compound CCCC(=O)OO LBAYFEDWGHXMSM-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 229920003986 novolac Polymers 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 150000004965 peroxy acids Chemical class 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- CZPZWMPYEINMCF-UHFFFAOYSA-N propaneperoxoic acid Chemical compound CCC(=O)OO CZPZWMPYEINMCF-UHFFFAOYSA-N 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Landscapes
- Epoxy Compounds (AREA)
- Epoxy Resins (AREA)
Description
(産業上の利用分野)
本発明は本質的にハロゲン基を含有しないエポ
キシ樹脂の製造方法に関するものである。
(従来技術)
従来、エレクトロニクス分野に於いて、エポキ
シ樹脂組成物が樹脂封止用、厚膜材料用、コーテ
イング用、封入用、接着用、レジスト用などに広
く応用されている。
しかも、近年LSIなどの開発によりエレクトロ
ニクス回路の精密化、微細化に伴い、これに組み
合わせて用いる樹脂系の材料の性能、特に長期の
耐熱、耐湿劣化、有害ガス発生などに伴う性能の
変動や部品の腐食などを抑えることが、従来にも
ましてより厳密に要求されるようになつて来た。
一方各種のエポキシ樹脂の中でも、ポリフエノ
ールのポリグリシジルエーテルタイプのものが最
も性能、作業性ともにバランスがとれ広くエレク
トロニクス分野に用いられている。
しかし、ポリフエノールのポリグリシジルエー
テルタイプのエポキシ樹脂に於いては、従来のポ
リフエノールとエピハロリドンとの反応によつて
いる限りは、必然的に微量(数百ppm程度)では
あるが、副生した加水分解性乃至非加水分解性ハ
ロゲン基を含有し、これが苛酷な実装条件などの
下での性能劣化の主原因となるのが最大の欠点と
されて来た。
一旦生成したハロゲン基は樹脂自体の一部分を
形成しているので、抽出、水洗、アルカリ水洗
滌、蒸留等の通常の精製方法では除去することは
本質的に不可能であり、通常の樹脂製造方法によ
つている限り避けることは出来ないものである。
(発明が解決しようとする課題)
本発明者らはこれらの点について種々検討の結
果、副反応としても全くハロゲン基を生成せず、
従つて本質的にハロゲン基を含有しないポリフエ
ノールのポリグリシジルエーテルタイプのエポキ
シ樹脂の新しい合成経路を見いだし、本発明をな
すに至つた。
即ち、本発明はビスフエノール類をアリルハラ
イドを用いて苛性アルカリ存在下に可及的にフエ
ノール性OH基がエーテル化されるまで反応さ
せ、分子当たり平均2.5個以上(好ましくは4.0個
以上)のアリル基を導入し、次に得られたポリア
リル化ビスフエノール類を有機過酸を用いてエポ
キシ化することにより、ハロゲン基を本質的に含
まないエポキシ樹脂を得んとするものである。
(課題を解決するための手段)
本発明に於いては有機過酸によりエポキシ化を
おこなう際、酸化され易い基を含んでいることは
望ましくないので、ビスフエノール類としてもビ
スフエノールA、ビスフエノールS、ビスフエノ
ールケトン、ビスフエノールエステル、ビスフエ
ノールエーテルなどが好ましい。
また、アリル化ビスフエノール類は重合性のア
リル基を有しているので各種の重合度のものが得
られる利点がある。半固形乃至固形樹脂を得るた
めには1.5〜100の重合度のオリゴマー乃至ポリマ
ー主体のものが好ましい。
ポリアリル化ビスフエノールの重合度はアリル
化の条件及びアリル重合反応の調整により得られ
るものである。
このように同一中間体をベースにしても、各種
の分子量並びに分子量分布の異なつたエポキシ樹
脂が容易に得られる点が本発明の特徴の一つであ
る。
このように本発明のエポキシ樹脂は、原料とし
てビスフエノール類をエピクロルヒドリンとの反
応により得られるいわゆる「エピビスタイプ」の
エポキシ樹脂に比し、エーテル型以外に核置換
型のエポキシ基をも有していてより多官能性であ
ること、不純物として有機のハロゲン基を本質
的に含まない代わりに、エーテル型及び核置換型
のアリル基を含んでいることが主な構造上の相違
点である。
なお、これらのアリル基は、重合性を有してお
り、従来のものに必然的に含まれた加水分解性乃
至非加水分解性の有機ハロゲン基のような悪い影
響は全く示さないものである。
なお、加水分解性ハロゲン基をアルカリ水で洗
滌して、ある水準まで除去精製すれば実用上差し
支えがないとされた時もあつたが、最近エレクト
ロニクス分野での樹脂の性能に対する要求がます
ます厳重になるにつれて、それでは不十分とな
り、今では非加水分解性ハロゲン基までも減少さ
せることが必要とされるようになつて来た。
しかも、単なるアルカリ水洗滌では樹脂の変質
を伴わないで、いわゆる非加水分解性ハロゲン基
までも大幅に減少させることは全く不可能であつ
た。
エレクトロニクス用エポキシ樹脂はハロゲン含
有量が30ppm以下(好ましくは10ppm以下)であ
ることが望ましく、本発明のエポキシ樹脂は本質
的にハロゲン来たを含まないのでこの水準までは
未反応アリルハライドの真空蒸留による溜去、水
洗などの通常の精製工程により容易に到達可能で
ある。
なお、従来法によるものでは如何に精製して
も、数百ppm、またはそれ以上のハロゲンを含ん
だ物しか得られなかつたことと比較すると、本発
明のエポキシ樹脂の工業的な利益は計り知れない
程大きいものである。
勿論その他のイオン性不純物についても問題は
ない。
本発明に用いるビスフエノール類は一般式
で示されるものであり、Xは有機過酸により酸化
されにくい基であることが必要である。
このためには−CH2−,−S−,−SO−,−NH
−,−CH2−O−CH2−,−O−CO−NH2−,−
CO−NH2−などの基は望ましくない。
本発明の目的のためにはXは
(Industrial Application Field) The present invention relates to a method for producing an epoxy resin that essentially does not contain halogen groups. (Prior Art) Conventionally, in the electronics field, epoxy resin compositions have been widely applied for resin sealing, thick film materials, coatings, encapsulation, adhesives, resists, and the like. Moreover, as electronic circuits become more precise and finer due to the development of LSIs in recent years, the performance of resin-based materials used in combination with these circuits has also been affected, especially due to long-term heat resistance, moisture resistance deterioration, and the generation of harmful gases. It has become more stringent than ever to suppress the corrosion of metals. On the other hand, among various epoxy resins, polyphenol polyglycidyl ether type resins have the best balance in both performance and workability and are widely used in the electronics field. However, in the polyglycidyl ether type epoxy resin of polyphenol, as long as it is based on the conventional reaction between polyphenol and epihalolidone, there is inevitably a small amount (about several hundred ppm) of by-products. The biggest drawback has been that it contains hydrolyzable or non-hydrolyzable halogen groups, which is the main cause of performance deterioration under severe packaging conditions. Once generated, the halogen group forms a part of the resin itself, so it is essentially impossible to remove it using normal purification methods such as extraction, washing with water, washing with alkaline water, and distillation. It cannot be avoided as long as it depends on the situation. (Problems to be Solved by the Invention) As a result of various studies on these points, the present inventors found that no halogen group is generated as a side reaction,
Therefore, a new synthetic route for a polyglycidyl ether type epoxy resin of polyphenol which essentially does not contain halogen groups was discovered, and the present invention was accomplished. That is, in the present invention, bisphenols are reacted with allyl halide in the presence of caustic alkali until as many phenolic OH groups as possible are etherified. By introducing an allyl group and then epoxidizing the obtained polyallylated bisphenols using an organic peracid, an epoxy resin essentially free of halogen groups is to be obtained. (Means for Solving the Problems) In the present invention, when performing epoxidation with an organic peracid, it is undesirable to contain groups that are easily oxidized, so bisphenols such as bisphenol A, bisphenol S, bisphenol ketone, bisphenol ester, bisphenol ether and the like are preferred. Furthermore, since allylated bisphenols have a polymerizable allyl group, they have the advantage of being available in various degrees of polymerization. In order to obtain a semi-solid to solid resin, a resin mainly composed of oligomers or polymers with a degree of polymerization of 1.5 to 100 is preferable. The degree of polymerization of polyallylated bisphenol can be obtained by adjusting the allylation conditions and the allylic polymerization reaction. One of the features of the present invention is that epoxy resins having various molecular weights and different molecular weight distributions can be easily obtained even if the same intermediate is used as a base. As described above, the epoxy resin of the present invention has nuclear substitution type epoxy groups in addition to ether type, compared to the so-called "epibis type" epoxy resin obtained by reacting bisphenols as raw materials with epichlorohydrin. The main structural differences are that it is more polyfunctional, and that it essentially does not contain organic halogen groups as impurities, but instead contains ether-type and nuclear-substituted allyl groups. These allyl groups are polymerizable and do not exhibit any negative effects unlike the hydrolyzable or non-hydrolyzable organic halogen groups that are naturally included in conventional products. . There was a time when it was thought that there would be no practical problem if the hydrolyzable halogen groups were removed and purified to a certain level by washing with alkaline water, but recently the demands on the performance of resins in the electronics field have become increasingly strict. As time progressed, this became insufficient, and it has now become necessary to reduce even non-hydrolyzable halogen groups. Furthermore, it has been impossible to significantly reduce even the so-called non-hydrolyzable halogen groups by simply washing with alkaline water without causing deterioration of the resin. It is desirable that the epoxy resin for electronics has a halogen content of 30 ppm or less (preferably 10 ppm or less), and since the epoxy resin of the present invention essentially does not contain halogen, up to this level, unreacted allyl halide can be vacuum distilled. This can be easily achieved through ordinary purification steps such as distillation and washing with water. The industrial benefits of the epoxy resin of the present invention are immeasurable when compared to conventional methods, which could only yield products containing several hundred ppm or more of halogen, no matter how much they were purified. It's so big that it doesn't exist. Of course, there is no problem with other ionic impurities. The bisphenols used in the present invention have the general formula It is necessary that X is a group that is not easily oxidized by organic peracids. For this purpose, −CH 2 −, −S−, −SO−, −NH
−, −CH 2 −O−CH 2 −, −O−CO−NH 2 −, −
Groups such as CO-- NH2- are undesirable. For the purposes of this invention, X is
【式】−SO2
−,−O−,−CO−,−CO−O−などが好ましい。
Xが酸化され易い基であると、エポキシ化の際
有機過酸の消費が過大になつたり、分子の解裂が
おこつたりするので望ましくない。
なお、上記の4,4′ジヒドロキシ化合物に対し
て、若干の2,2′、2,4′、3,3′、2,3′、3,
4′などの異性体を併用してもよい。
本発明に用いるポリアリル化ビスフエノール類
は通常、上記のビスフエノール類とアリルハライ
ドとを苛性アルカリ存在下で反応させて、フエノ
ール性OHをアリルエーテル化すると共に、その
クライゼン転位をも行わせて核置換のアリル基を
も導入したものである。
分子当たりのアリル基は、理論的には6.0個ま
で導入可能であり、本発明の目的のためには2.5
個以上(好ましくは4.0個以上)導入されている
ことが多官能性のものを得るために必要である。
更に本発明に用いるポリアリル化ビスフエノー
ル類は可及的にフリーのフエノール性OH基を含
んでいないことが必要である。
フリーのフエノール性OH基が多く残つている
と、官能性が低下すること、有機過酸による
エポキシ化の際異常に過酸が多く消費されること
などにより極めて不利である。
なお、ポリアリル化ビスフエノールに残存する
フリーのフエノール性OH基は低級アルキルハラ
イドや低級脂肪酸などと反応させ消失させてもよ
い。
本発明に於いては、残存フエノール性OH基は
0.2個/核以下であることが好まい。
本発明のポリアリル化ビスフエノール類は通常
の製造条件ではアリル基による重合は殆どおこら
ない。
しかし、半固形乃至固形のエポキシ樹脂を目的
とする場合には、数平均重合度が1.5〜100のもの
(好ましくは3.0〜50のもの)が望ましい。これよ
り分子量が増大すると反応の調整が困難となるの
で好ましくない。
本発明のポリアリル化ビスフエノール類の高分
子化は通常アリル基の重合によつて行うことが出
来る。
即ち、空気中で高温(例えば200℃以上)で攪
拌するとか、ラジカル重合開始剤を用いて溶液中
で重合させるとかしてもよい。
但し、ポリアリル化ビスフエノール類は多官能
性であるから重合反応を適宜抑制するとか、重合
率の低いところで反応を停止させ重合物を分別す
るとかしないと、ゲル化物を多量に生成する恐れ
があるので望ましくない。
本発明に用いるポリアリル化ビスフエノール類
は上記の要件を充しているならば製造法如何に拘
わらず、いずれもほぼ同様に用いることが出来
る。
本発明に於けるポリアリル化ビスフエノール類
(オリゴマー、ポリマーをも含む)有機過酸によ
つてアリル基のエポキシ化を行う。
有機過酸としては過酢酸が最も適当であるが、
過安息香酸モノ過フタル酸(m,pの異性体をも
含む)、トリフルオロ過酢酸、過プロピオン酸、
過酪酸、モノ過コハク酸などを用いても良い。
また、20〜35%の過酸化水素水とギ酸、酢酸な
ど望ましい低級脂肪酸の混合液の形で用いてもよ
い。
反応温度は高いと爆発の危険性があるので、50
℃以下(好ましくは室温またはそれ以下)で反応
させることが好ましい。
(実施例)
実施例 1
ビスフエノールS125部、苛性ソーダ80部をエ
チルセルソルブ1000部に溶解し、還流、攪拌下塩
化アリル56.5部を80℃、1時間で滴下し、次いで
一部溶剤を留出させつつ220℃まで昇温させる。
つぎに留出した溶剤を系にもどし、再び塩化ア
リル76.5部を80℃、1時間で滴下する。
次にベンゾイルパーオキサイド0.2部を加え、
80℃で1時間重合させて後、水洗して食塩を除去
し、溶剤を減圧下除去する(収量:240部)。
得られたポリアリル化ビスフエノールは室温で
固形であり、数平均重合度:4.7、アリル基の
数/分子:10.2、フリーのフエノール性OH基/
核:0.2であつた。
ポリアリル化ビスフエノール110部を酢酸メチ
ル500部に溶解し、過酢酸110部を0℃で加え殆ど
消費するまで反応させる。
次に水洗と減圧蒸留により精製する(収量:
103部)
得られたエポキシ樹脂は、室温で固形で軟化点
が80℃であり、エポキシ当量180、エポキシ基の
数/分子:8.8であつた。
また全ハロゲン含有量(酸素ボンベ法)は
25ppmであつた。
(発明の効果)
本発明のエポキシ樹脂は、つぎのような特徴を
有している。
高分子主体のものでは固形であり、分子量の
増大と共にエポキシ基及びアリル基の数(分子
当たり)、即ち官能性は増大する傾向があるこ
と。(エピビス系並びにエポキシ化ノボラツク
系と相違する点である。)
分子量が高くなつても、軟化点はあまり高く
ならず、しかも溶解性や他のポリマーへの相溶
性が劣化しないこと。
本質的に有機のハロゲン基を含有していない
こと。
従つて本発明のエポキシ樹脂は従来のエポキシ
樹脂とは本質的に異なるものであり、特にエレク
トロニクス業界への応用分野に於いて、その特徴
が生かされるので工業的価値の極めて高いもので
ある。[Formula] -SO 2 -, -O-, -CO-, -CO-O-, etc. are preferred. If X is a group that is easily oxidized, it is undesirable because the organic peracid will be consumed excessively during epoxidation or the molecule will be cleaved. In addition, for the above 4,4' dihydroxy compound, some 2,2', 2,4', 3,3', 2,3', 3,
Isomers such as 4′ may also be used in combination. The polyallylated bisphenols used in the present invention are usually produced by reacting the above-mentioned bisphenols with allyl halide in the presence of caustic alkali to convert the phenolic OH into allyl ether, and also to undergo Claisen rearrangement. A substituted allyl group is also introduced. Theoretically, up to 6.0 allyl groups can be introduced per molecule, and for the purpose of the present invention, 2.5 allyl groups can be introduced per molecule.
In order to obtain a polyfunctional product, it is necessary to introduce at least 4.0 (preferably 4.0 or more). Furthermore, it is necessary that the polyallylated bisphenols used in the present invention contain as few free phenolic OH groups as possible. If a large amount of free phenolic OH groups remain, it is extremely disadvantageous because the functionality decreases and an abnormally large amount of peracid is consumed during epoxidation with an organic peracid. Note that free phenolic OH groups remaining in the polyallylated bisphenol may be eliminated by reacting with a lower alkyl halide, lower fatty acid, or the like. In the present invention, residual phenolic OH groups are
The number is preferably 0.2/nucleus or less. In the polyallylated bisphenols of the present invention, polymerization by allyl groups hardly occurs under normal production conditions. However, when a semi-solid to solid epoxy resin is intended, it is desirable that the number average degree of polymerization is 1.5 to 100 (preferably 3.0 to 50). If the molecular weight increases more than this, it becomes difficult to control the reaction, which is not preferable. Polymerization of the polyallylated bisphenols of the present invention can usually be carried out by polymerization of allyl groups. That is, the mixture may be stirred in the air at a high temperature (for example, 200° C. or higher) or polymerized in a solution using a radical polymerization initiator. However, since polyallylated bisphenols are polyfunctional, unless the polymerization reaction is appropriately suppressed or the reaction is stopped at a low polymerization rate and the polymer is separated, there is a risk of producing a large amount of gelled product. Therefore, it is undesirable. As long as the polyallylated bisphenols used in the present invention satisfy the above requirements, they can be used in almost the same way regardless of the manufacturing method. In the present invention, polyallylated bisphenols (including oligomers and polymers) are epoxidized with an organic peracid. Peracetic acid is the most suitable organic peracid, but
perbenzoic acid monoperphthalic acid (including m and p isomers), trifluoroperacetic acid, perpropionic acid,
Perbutyric acid, monopersuccinic acid, etc. may also be used. Alternatively, it may be used in the form of a mixed solution of 20 to 35% hydrogen peroxide and a desirable lower fatty acid such as formic acid or acetic acid. If the reaction temperature is high, there is a risk of explosion, so 50
It is preferable to carry out the reaction at a temperature below .degree. C. (preferably at room temperature or below). (Example) Example 1 125 parts of bisphenol S and 80 parts of caustic soda were dissolved in 1000 parts of ethyl cellosolve, and 56.5 parts of allyl chloride was added dropwise at 80°C for 1 hour under reflux and stirring, and then some of the solvent was distilled off. While heating, raise the temperature to 220℃. Next, the distilled solvent is returned to the system, and 76.5 parts of allyl chloride is again added dropwise at 80°C over 1 hour. Next, add 0.2 parts of benzoyl peroxide,
After polymerizing at 80°C for 1 hour, the salt was removed by washing with water, and the solvent was removed under reduced pressure (yield: 240 parts). The obtained polyallylated bisphenol is solid at room temperature, number average degree of polymerization: 4.7, number of allyl groups/molecule: 10.2, free phenolic OH group/
Nucleus: 0.2. 110 parts of polyallylated bisphenol is dissolved in 500 parts of methyl acetate, and 110 parts of peracetic acid is added at 0°C and reacted until almost consumed. Next, it is purified by water washing and vacuum distillation (yield:
(103 parts) The obtained epoxy resin was solid at room temperature, had a softening point of 80°C, had an epoxy equivalent of 180, and number of epoxy groups/molecule: 8.8. In addition, the total halogen content (oxygen cylinder method) is
It was 25ppm. (Effects of the Invention) The epoxy resin of the present invention has the following characteristics. Those based on polymers are solid, and as the molecular weight increases, the number of epoxy groups and allyl groups (per molecule), that is, the functionality tends to increase. (This is different from Epibis type and epoxidized novolac type.) Even if the molecular weight becomes high, the softening point does not increase too much, and solubility and compatibility with other polymers do not deteriorate. Contains essentially no organic halogen groups. Therefore, the epoxy resin of the present invention is essentially different from conventional epoxy resins, and has extremely high industrial value because its characteristics can be utilized particularly in the field of application to the electronics industry.
Claims (1)
ルハライドとを苛性アルカリの存在下で反応させ
たポリアリル化ビスフエノールに、更にアリル基
を加熱又はラジカル重合開始剤を用いて重合させ
て得られる数平均重合度が1.5〜100のオリゴマー
乃至ポリマーを有機化酸によりエポキシ化する方
法において、ポリアリル化ビスフエノールはアリ
ル基をビスフエノール1分子当たり平均2.5個以
上有し、しかもフリーのフエノール性OH基を可
及的に含まないものを用いることを特徴とする半
固形乃至固形のエポキシ系樹脂の製造方法。 X;【式】−SO2−,−O−,−CO− COO−を示す。[Scope of Claims] 1 Polyallylated bisphenol obtained by reacting bisphenols represented by the formula [] with allyl halide in the presence of caustic alkali is further polymerized with an allyl group by heating or using a radical polymerization initiator. In the method of epoxidizing oligomers or polymers with a number average degree of polymerization of 1.5 to 100 obtained by epoxidizing with an organic acid, polyallylated bisphenols have an average of 2.5 or more allyl groups per bisphenol molecule and are free. A method for producing a semi-solid to solid epoxy resin, characterized in that a resin containing as little phenolic OH group as possible is used. X: [Formula] -SO 2 -, -O-, -CO- COO-.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13158189A JPH0214212A (en) | 1989-05-26 | 1989-05-26 | Production of epoxy resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13158189A JPH0214212A (en) | 1989-05-26 | 1989-05-26 | Production of epoxy resin |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4883A Division JPS59124905A (en) | 1983-01-05 | 1983-01-05 | Production of epoxy resin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0214212A JPH0214212A (en) | 1990-01-18 |
| JPH0375563B2 true JPH0375563B2 (en) | 1991-12-02 |
Family
ID=15061402
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13158189A Granted JPH0214212A (en) | 1989-05-26 | 1989-05-26 | Production of epoxy resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0214212A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PL2281947T5 (en) | 2009-06-26 | 2023-03-06 | Joseph Vögele AG | Road finisher with automatic motor control |
-
1989
- 1989-05-26 JP JP13158189A patent/JPH0214212A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0214212A (en) | 1990-01-18 |
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