JPS5817529B2 - Manufacturing method of novolak resin - Google Patents
Manufacturing method of novolak resinInfo
- Publication number
- JPS5817529B2 JPS5817529B2 JP323279A JP323279A JPS5817529B2 JP S5817529 B2 JPS5817529 B2 JP S5817529B2 JP 323279 A JP323279 A JP 323279A JP 323279 A JP323279 A JP 323279A JP S5817529 B2 JPS5817529 B2 JP S5817529B2
- Authority
- JP
- Japan
- Prior art keywords
- pinene
- novolak resin
- isomerized
- adduct
- formaldehyde
- 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
- 229920003986 novolac Polymers 0.000 title claims description 13
- 229920005989 resin Polymers 0.000 title claims description 11
- 239000011347 resin Substances 0.000 title claims description 11
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- GRWFGVWFFZKLTI-IUCAKERBSA-N (-)-α-pinene Chemical compound CC1=CC[C@@H]2C(C)(C)[C@H]1C2 GRWFGVWFFZKLTI-IUCAKERBSA-N 0.000 claims description 26
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 26
- MVNCAPSFBDBCGF-UHFFFAOYSA-N alpha-pinene Natural products CC1=CCC23C1CC2C3(C)C MVNCAPSFBDBCGF-UHFFFAOYSA-N 0.000 claims description 13
- GRWFGVWFFZKLTI-UHFFFAOYSA-N rac-alpha-Pinene Natural products CC1=CCC2C(C)(C)C1C2 GRWFGVWFFZKLTI-UHFFFAOYSA-N 0.000 claims description 13
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 claims description 11
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 9
- 230000002378 acidificating effect Effects 0.000 claims description 5
- 239000003054 catalyst Substances 0.000 claims description 5
- 235000006408 oxalic acid Nutrition 0.000 claims description 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 8
- 239000012778 molding material Substances 0.000 description 8
- 230000018044 dehydration Effects 0.000 description 4
- 238000006297 dehydration reaction Methods 0.000 description 4
- 238000010292 electrical insulation Methods 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000004312 hexamethylene tetramine Substances 0.000 description 1
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- GEVPUGOOGXGPIO-UHFFFAOYSA-N oxalic acid;dihydrate Chemical compound O.O.OC(=O)C(O)=O GEVPUGOOGXGPIO-UHFFFAOYSA-N 0.000 description 1
- 229920002866 paraformaldehyde Polymers 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
Landscapes
- Phenolic Resins Or Amino Resins (AREA)
Description
【発明の詳細な説明】 この発明はノボラック樹脂の製法に関する。[Detailed description of the invention] This invention relates to a method for producing novolac resins.
従来、フェノール樹脂成形材料は、一般に、フェノール
とホルムアルデヒドとを酸性触媒の存在下で反応させ、
さらに減圧脱水を行うことによって得たノボラック樹脂
と、ヘキサメチレンテトラミン等の硬化剤および充填剤
その他とを加熱、混練し粉砕することによって得ていた
。Conventionally, phenolic resin molding materials are generally produced by reacting phenol and formaldehyde in the presence of an acidic catalyst.
The novolac resin obtained by further dehydration under reduced pressure, a curing agent such as hexamethylenetetramine, a filler, and the like were heated, kneaded, and pulverized.
しかしながら、上記従来の成形材料には、つぎのような
欠点があった。However, the above-mentioned conventional molding materials had the following drawbacks.
すなわち、ノボラック樹脂中に7%以上も残存する未反
応フェノールの大部分が減圧脱水工程中に留出するため
、省資源という観点からは無駄がありかつその処理が必
要となるほか、留出することなく成形材料中に残ったフ
ェノールが成形品中に移るため成形品が高温中にさらさ
れると気化することによって成形品の外観や性能を損う
等成形品の耐熱性を低下させ、さらにフェノールが親水
性であるため成形品の電気絶縁性を低下させるという不
利益もあった。In other words, most of the unreacted phenol that remains in the novolak resin (more than 7%) is distilled out during the vacuum dehydration process, which is wasteful from the perspective of resource conservation and requires treatment. Phenol remaining in the molding material transfers into the molded product without leaving the molding material, so when the molded product is exposed to high temperatures, it evaporates, impairing the appearance and performance of the molded product, reducing the heat resistance of the molded product, and further reducing the phenol content. Since it is hydrophilic, it also has the disadvantage of reducing the electrical insulation properties of the molded product.
この発明は主としてこのような問題を解決するために工
夫されたものであるが、しかし、この発明の実施によっ
て得られるノボラック樹脂は成形材料の製造用以外の用
途にも使用される。Although this invention was devised primarily to solve these problems, the novolak resin obtained by implementing this invention can also be used for purposes other than the production of molding materials.
この発明はフェノールを、下記〔I〕で表わされる異性
化α−ピネンの2付加物
の形で用いることによって上記目的を達成しようとする
ものであって、異性化α−ピネンのジフェノール付加物
とホルムアルデヒドとを酸性触媒の存在下で反応させる
ことを特徴とするノボラック樹脂の製法をその要旨とす
る。This invention aims to achieve the above object by using phenol in the form of a di-adduct of isomerized α-pinene represented by [I] below, which is a diphenol adduct of isomerized α-pinene. The gist is a method for producing a novolak resin, which is characterized by reacting formaldehyde with formaldehyde in the presence of an acidic catalyst.
異性化α−ピネンのジフェノール付加物は高温下におい
ても安定であるため、ホルムアルデヒドと反応させるべ
きフェノール源として、このよりなα−ピネンとの付加
物を用いたときには、未反応物として樹脂中に残存する
異性化α−ピネンのジフェノール付加物は、減圧脱水工
程に際しても留出することがないため、処理の必要がな
く、かつ、このものは成形品中に残り、硬化した樹脂の
構造中に組み込まれて有効に使用される。The diphenol adduct of isomerized α-pinene is stable even at high temperatures, so when this adduct with α-pinene is used as a phenol source to be reacted with formaldehyde, it remains in the resin as an unreacted product. The diphenol adduct of isomerized α-pinene that remains in the resin does not distill out during the vacuum dehydration process, so there is no need to treat it. be incorporated into the system and used effectively.
しかも、異性化α−ピネンのジフェノールft1JDe
lはフェノールに比べて疎水性であるため、成形品の電
気絶縁性を低下させることがない。Moreover, the diphenol ft1JDe of isomerized α-pinene
Since l is more hydrophobic than phenol, it does not reduce the electrical insulation properties of the molded product.
異性化α−ピネンのジフェノール付加物cI:]は、た
とえば、つぎのようにして合成され、安原油脂工業株式
会社製商品名「シルバー7」として入手できる。The diphenol adduct cI of isomerized α-pinene is synthesized, for example, as follows, and is available under the trade name “Silver 7” manufactured by Yasushi Oil Industries Co., Ltd.
異性化α−ピネンのジフェノール付加物は、下記のよう
な化合物CM)、[1II)が混入した形で使用されろ
こともある。The diphenol adduct of isomerized α-pinene may be used in a mixed form with the following compounds CM), [1II).
ホルムアルデヒド源としてはホルマリンやパラホルムな
どが用いられる。Formaldehyde sources such as formalin and paraform are used.
ホルムアルデヒドは、特にこれに限定されるという趣旨
ではないが、通常、異性化α−ピネンのジフェノール付
加物1モルに対し10〜1.8モル、好ましくは1.2
71.6モルの割合で使用される。Although formaldehyde is not particularly limited to this, it is usually 10 to 1.8 mol, preferably 1.2 mol, per mol of the diphenol adduct of isomerized α-pinene.
It is used in a proportion of 71.6 moles.
酸性触媒は、蓚酸、塩酸等ノボラック樹脂の製造用とし
て一般に使用されているものが、この発明においても使
用される。As acidic catalysts, those commonly used for producing novolac resins, such as oxalic acid and hydrochloric acid, are also used in this invention.
この場合にも、特にこれに限定されるという趣旨ではな
し・が、たとえば、蓚酸が使用される場合には、このも
のが異性化α−ピネンのジフェノール付加物1モルに対
し0.002〜0004モルの割合で使用される。In this case as well, it is not meant to be limited to this. For example, when oxalic acid is used, the amount of this acid is 0.002 to 1 mol per mol of the diphenol adduct of isomerized α-pinene. 0004 mol.
これらの原料を用いてノボラック樹脂をつくる方法は、
公知のとおりである。The method of making novolac resin using these raw materials is as follows.
As is known.
この発明は上記のように構成されるため、この発明の実
施によって得られたノボラック樹脂をたとえば成形材料
の製造に用いると、耐熱性が良く電気絶縁性の高い成形
品をつくることができる。Since the present invention is configured as described above, when the novolak resin obtained by carrying out the present invention is used, for example, in the production of a molding material, a molded article with good heat resistance and high electrical insulation can be produced.
つぎに、実施例を従来例と併せて説明する。Next, an embodiment will be described together with a conventional example.
四つ目フラスコに、第1表記載のフェノール成分と、5
5%ホルマリンと、蓚酸2水塩とを同表記載の量だけと
り、攪拌機、温度計および還流冷却器を付して加熱下撹
拌を行い、約30分を要して内容物を沸騰させ、以後沸
騰状態下で35時間攪拌を続けたのち、冷却器を取り換
えて60分を要して減圧上脱水を行い、その後160℃
まで昇温させ、約30分開城圧下攪拌してノボラック樹
1旨を得た。In a fourth flask, add the phenol components listed in Table 1 and 5
Take 5% formalin and oxalic acid dihydrate in the amounts listed in the same table, add a stirrer, a thermometer, and a reflux condenser, stir under heat, and bring the contents to a boil over about 30 minutes. After that, stirring was continued for 35 hours under boiling conditions, the cooler was replaced and dehydration was performed under reduced pressure for 60 minutes, and then the temperature was increased to 160°C.
The mixture was heated to a temperature of 100.degree. C. and stirred under pressure for about 30 minutes to obtain a novolac tree.
この樹脂を用℃・て、第1表記載の配合割合で配合した
原材料を常法に従って加熱ロールにより混練し、つぎに
粉砕して成形材料とした。Using this resin, raw materials blended at the mixing ratios shown in Table 1 were kneaded using heated rolls according to a conventional method, and then ground to obtain a molding material.
上記で得られた三種の成形材料を用いて、常法に従い直
圧成形によって成形品を得た。Using the three types of molding materials obtained above, molded products were obtained by direct pressure molding according to a conventional method.
各成形品の性能は第2表に示すとおりであり、実施例の
ものの耐熱性および電気絶縁性は、(・ずれも、従従例
のもののそれらよりすぐれていることがわかる。The performance of each molded product is shown in Table 2, and it can be seen that the heat resistance and electrical insulation properties of the molded products of the examples are superior to those of the conventional examples.
Claims (1)
ルデヒドとを酸性触媒の存在下で反応させることを特徴
とするノボラック樹脂の製法。 2 ホルムアルデヒドが異性化α−ピネンのジフェノー
ル付加物1モルに対し1.0〜1.8モルの割合で使用
される特許請求の範囲第1項記載のノボラック樹脂の製
法。 3 酸性触媒として、蓚酸が、異性化α−ピネンのジフ
ェノール付加物1モルに対し0.002〜0.004モ
ルの割合で使用される特許請求の範囲第1項記載のノボ
ラック樹脂の製法。[Scope of Claims] 1. A method for producing a novolak resin, which comprises reacting a diphenol adduct of isomerized α-pinene with formaldehyde in the presence of an acidic catalyst. 2. The method for producing a novolak resin according to claim 1, wherein formaldehyde is used in a ratio of 1.0 to 1.8 mol per mol of the diphenol adduct of isomerized α-pinene. 3. The method for producing a novolak resin according to claim 1, wherein oxalic acid is used as the acidic catalyst in a ratio of 0.002 to 0.004 mol per mol of the diphenol adduct of isomerized α-pinene.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP323279A JPS5817529B2 (en) | 1979-01-13 | 1979-01-13 | Manufacturing method of novolak resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP323279A JPS5817529B2 (en) | 1979-01-13 | 1979-01-13 | Manufacturing method of novolak resin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5594921A JPS5594921A (en) | 1980-07-18 |
| JPS5817529B2 true JPS5817529B2 (en) | 1983-04-07 |
Family
ID=11551694
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP323279A Expired JPS5817529B2 (en) | 1979-01-13 | 1979-01-13 | Manufacturing method of novolak resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5817529B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2572293B2 (en) * | 1990-05-23 | 1997-01-16 | 油化シェルエポキシ株式会社 | Epoxy resin curing agent and curable epoxy resin composition |
| JP6137559B2 (en) * | 2014-03-20 | 2017-05-31 | 荒川化学工業株式会社 | Rosin-modified phenolic resin, resin varnish for printing ink and printing ink |
-
1979
- 1979-01-13 JP JP323279A patent/JPS5817529B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5594921A (en) | 1980-07-18 |
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