Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0611779B2 - Thermosetting resin manufacturing method - Google Patents
[go: Go Back, main page]

JPH0611779B2 - Thermosetting resin manufacturing method - Google Patents

Thermosetting resin manufacturing method

Info

Publication number
JPH0611779B2
JPH0611779B2 JP60034199A JP3419985A JPH0611779B2 JP H0611779 B2 JPH0611779 B2 JP H0611779B2 JP 60034199 A JP60034199 A JP 60034199A JP 3419985 A JP3419985 A JP 3419985A JP H0611779 B2 JPH0611779 B2 JP H0611779B2
Authority
JP
Japan
Prior art keywords
resin
reaction
tung oil
added
weight
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 - Fee Related
Application number
JP60034199A
Other languages
Japanese (ja)
Other versions
JPS61192712A (en
Inventor
優 緒方
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP60034199A priority Critical patent/JPH0611779B2/en
Publication of JPS61192712A publication Critical patent/JPS61192712A/en
Publication of JPH0611779B2 publication Critical patent/JPH0611779B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Phenolic Resins Or Amino Resins (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、常温打抜き加工性、耐薬品性を必要とする積
層板の製造に有効な熱硬化性樹脂の製造法に関する。
TECHNICAL FIELD The present invention relates to a method for producing a thermosetting resin which is effective for producing a laminated plate that requires room temperature punching workability and chemical resistance.

従来の技術 従来、打抜き加工性を必要とする積層板には、桐油変性
フェノール樹脂が用いられている。桐油変性フェノール
樹脂は、フェノール類と桐油を酸性触媒下で反応させた
後ホルムアルデヒド類を添加し塩基性触媒下でレゾール
化反応を進めたものである。この桐油変性フェノール樹
脂には、リン酸エステル化合物を添加して積層板の低温
打抜き加工性を良くすることが行なわれている。
2. Description of the Related Art Conventionally, tung oil-modified phenolic resin has been used for a laminated plate which requires punching workability. The tung oil-modified phenolic resin is obtained by reacting phenols with tung oil under an acidic catalyst and then adding formaldehyde to proceed the resolization reaction under a basic catalyst. A phosphoric acid ester compound is added to the tung oil-modified phenolic resin to improve the low temperature punching workability of the laminated plate.

発明が解決しようとする問題点 しかし、リン酸エステル化合物の添加量を多くすると、
積層板の低温打抜き加工性は向上するが、高温域での層
間密着性が低下し、耐薬品性も著しく低下する欠点があ
る。一方、リン酸エステル化合物の添加量が少ない場合
には、打抜き温度範囲が狭くなり、リン酸エステル化合
物を添加しているから耐薬品性も多少低下する。
Problems to be Solved by the Invention However, if the addition amount of the phosphate ester compound is increased,
Although the low temperature punching workability of the laminated plate is improved, there is a drawback that the interlayer adhesion in the high temperature region is lowered and the chemical resistance is also remarkably lowered. On the other hand, when the addition amount of the phosphoric acid ester compound is small, the punching temperature range is narrowed and the chemical resistance is somewhat lowered because the phosphoric acid ester compound is added.

本発明は、常温打抜き加工性、耐薬品性の優れた積層板
の製造に有効な桐油変性フェノール樹脂を提供すること
を目的とする。
It is an object of the present invention to provide a tung oil-modified phenolic resin which is effective in producing a laminate having excellent room-temperature punchability and chemical resistance.

問題点を解決するための手段 上記目的を達成するために本発明は、フェノール類と桐
油を酸性触媒下で反応させた後ホルムアルデヒド類を添
加し塩基性触媒下でレゾール化反応を進める桐油変性フ
ェノール樹脂の製造に於いて、レゾール化反応時にリン
酸エステル化合物を添加し、反応終点の高分子量物(
≒4000)が反応生成物中の20〜25重量%の範囲
内になる様することを特徴とするものである。
Means for Solving the Problems In order to achieve the above object, the present invention relates to a tung oil-modified phenol in which phenols and tung oil are reacted under an acidic catalyst and then formaldehydes are added to proceed a resolization reaction under a basic catalyst. In the production of resin, a phosphoric acid ester compound is added during the resolization reaction to produce a high molecular weight compound (
≈4000) in the range of 20 to 25% by weight in the reaction product.

作用 本発明は、生成した桐油変性フェノール樹脂にリン酸エ
ステル化合物を添加するのではなく、桐油変性フェノー
ル樹脂を得る反応過程に於いてレゾール化反応時にリン
酸エステル化合物を添加することによって、常温打抜き
加工性、耐薬品の優れた積層板の製造に有効な桐油変性
フェノール樹脂が得られるのである。尚、反応終点の高
分子量物(≒4000)の量が20重量%未満のとき
は、積層板の耐薬品性、高温での層間密着性が悪くな
る。一方、前記高分子量物が25重量%を越えると反応
生成物の粘度が急上昇して生産性に問題があり、また、
積層板としたときの硬さが増して打抜き加工性が低下す
る(高温打抜きとなる)。
Effect The present invention does not add a phosphate ester compound to the produced tung oil-modified phenol resin, but adds a phosphate ester compound during the resolization reaction in the reaction process for obtaining a tung oil-modified phenol resin, thereby punching at room temperature. Thus, a tung oil-modified phenolic resin which is effective for producing a laminate having excellent processability and chemical resistance can be obtained. When the amount of the high molecular weight substance (≈4000) at the end of the reaction is less than 20% by weight, the chemical resistance of the laminate and the interlayer adhesion at high temperature are deteriorated. On the other hand, if the amount of the high molecular weight compound exceeds 25% by weight, the viscosity of the reaction product will sharply increase and there will be a problem in productivity.
When it is made into a laminated plate, the hardness is increased and the punching workability is deteriorated (it becomes a high temperature punching).

実施例 本発明を実施するに当り、レゾール化反応に於いてフェ
ノール類とホルムアルデヒド類のモル比は、フェノール
類1モルに対してホルムアルデヒド類1.1〜1.5モルが好
ましい。本発明により得られた桐油変性フェノール樹脂
は、紙等の基材に含浸乾燥してプリプレグとし、これを
所定枚数重ね加熱加圧成形して積層板とする。
EXAMPLES In carrying out the present invention, the molar ratio of phenols to formaldehydes in the resolization reaction is preferably 1.1 to 1.5 moles of formaldehydes to 1 mole of phenols. The tung oil-modified phenolic resin obtained according to the present invention is impregnated into a base material such as paper and dried to form a prepreg, and a predetermined number of the prepreg are laminated and heat-pressed to form a laminate.

以下実施例を述べる。Examples will be described below.

実施例1 まず、フェノール864g、オルソクレゾール96g、
桐油517g、パラトルエンスルホン酸を三ツ口フラス
コに投入し、80℃で90分反応させた。次に、86%
パラホルムアルデヒド422g、トリエチルアミン38
gを添加し、レゾール化反応1時間後にリン酸エステル
(商品名:レオフォス)を添加して更に反応を進めて、
生成物中の高分子量物(≒4000)が20重量%の
樹脂を得た。この樹脂にメタノールを添加し、樹脂固型
50重量%のワニスとし、11ミルスの紙基材に含浸乾
燥して樹脂量47%のプリプレグを作り、このプリプレ
グを8枚重ね160℃−100Kg/cm2の圧力下で60
分加熱加圧して1.6mm厚の銅張り積層板を得た。
Example 1 First, 864 g of phenol, 96 g of orthocresol,
517 g of tung oil and p-toluenesulfonic acid were put into a three-necked flask and reacted at 80 ° C. for 90 minutes. Next, 86%
Paraformaldehyde 422g, triethylamine 38
g, and after 1 hour of the resolization reaction, a phosphoric acid ester (trade name: Reophos) was added to further advance the reaction,
A resin having a high molecular weight (≈4000) in the product of 20% by weight was obtained. Methanol was added to this resin to form a resin-solidified 50% by weight varnish, which was impregnated into an 11 mils paper base material and dried to form a prepreg with a resin amount of 47%. 60 under pressure of 2
After heating and pressurizing for a minute, a 1.6 mm thick copper clad laminate was obtained.

尚、反応生成物の分子量の測定は、高速液体クロマトグ
ラフ分析による。
The molecular weight of the reaction product is measured by high performance liquid chromatography analysis.

実施例2 実施例1と同様にレゾール化反応を進め、生成物中の高
分子量物(≒4000)25重量%の樹脂を得た。こ
の樹脂にメタノールを添加し、樹脂固型50重量%と
し、実施例1と同様にして1.6mm厚の銅張り積層板を得
た。
Example 2 The resolization reaction was carried out in the same manner as in Example 1 to obtain a resin containing 25% by weight of a high molecular weight substance (≈4000) in the product. Methanol was added to this resin to make the resin solid type 50% by weight, and a copper clad laminate having a thickness of 1.6 mm was obtained in the same manner as in Example 1.

比較例1 実施例1と同様にしてレゾール化反応を進め、生成物中
の高分子量物(≒4000)26重量%の樹脂を得
た。但し、この樹脂は粘度が高く、メタノールを添加し
ても溶解するのに長時間を要した。このワニスを用い実
施例1と同様にして1.6mm厚の銅張り積層板を得た。
Comparative Example 1 The resolization reaction was carried out in the same manner as in Example 1 to obtain a resin having a high molecular weight (≈4000) of 26% by weight in the product. However, this resin had a high viscosity, and it took a long time to dissolve even if methanol was added. Using this varnish, a copper-clad laminate having a thickness of 1.6 mm was obtained in the same manner as in Example 1.

比較例2 実施例1と同様レゾール化反応を進め、生成物中の高分
子量物(≒4000)が19重量%の樹脂を得た。こ
の樹脂にメタノールを添加し、樹脂固型50重量%と
し、実施例1と同様にして1.6mm厚の銅張り積層板を得
た。
Comparative Example 2 The resolization reaction was carried out in the same manner as in Example 1 to obtain a resin in which the high molecular weight substance (≈4000) in the product was 19% by weight. Methanol was added to this resin to make the resin solid type 50% by weight, and a copper clad laminate having a thickness of 1.6 mm was obtained in the same manner as in Example 1.

従来例 まず、フェノール864g、オルソクレゾール96g、
桐油517g、パラトルエンスルホン酸を三ツ口フラス
コに投入し、80℃で90分反応させた。次に、86%
パラホルムアルデヒド316g、37%ホルマリン24
5g、トリメチルアミン30gを投入し70℃でレゾー
ル化反応を行ない、ゲルタイム6分〜6分30秒の時点
で脱水を行なった。脱水終了後、実施例1と同様のリン
酸エステル及びメタノールを添加し、樹脂固型50重量
%のワニスとし実施例1と同様にして1.6mm厚の銅張り
積層板を得た。
Conventional example First, phenol 864g, orthocresol 96g,
517 g of tung oil and p-toluenesulfonic acid were put into a three-necked flask and reacted at 80 ° C. for 90 minutes. Next, 86%
Paraformaldehyde 316g, 37% formalin 24
5 g and 30 g of trimethylamine were added, a resolization reaction was performed at 70 ° C., and dehydration was performed at a gel time of 6 minutes to 6 minutes 30 seconds. After completion of the dehydration, the same phosphoric acid ester and methanol as in Example 1 were added to obtain a resin-solidified 50% by weight varnish, and in the same manner as in Example 1, a 1.6 mm-thick copper clad laminate was obtained.

前記実施例、比較例及び従来例で得た積層板の特性を第
1表に示す。
Table 1 shows the characteristics of the laminates obtained in the above Examples, Comparative Examples and Conventional Examples.

発明の効果 第1表から明らかな様に、本発明による熱硬化性樹脂を
使用した積層板は、常温打抜き加工性、耐薬品性を兼ね
合せ保持している。これは、桐油変性フェノール樹脂生
成中のレゾール化反応の過程に於いてリン酸エステル化
合物を添加し、生成物中の高分子量物(≒4000)
が20〜25重量%の範囲内にする事によって達成出来
たものである。
EFFECTS OF THE INVENTION As is clear from Table 1, the laminate using the thermosetting resin according to the present invention has both room temperature stamping workability and chemical resistance. This is because the phosphoric acid ester compound was added in the process of the resolization reaction during the production of tung oil-modified phenolic resin, and the high molecular weight product (≈4000) in the product
Can be achieved by adjusting the content of the compound in the range of 20 to 25% by weight.

また、耐熱性等も特に問題なく、電子機器分野で特に必
要とする特性を充分満足する積層板を提供できる点、そ
の工業的価値は極めて大である。
In addition, there is no particular problem with heat resistance and the like, and it is possible to provide a laminated plate that sufficiently satisfies the properties particularly required in the electronic device field, and its industrial value is extremely large.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】フェノール類と桐油を酸性触媒下で反応さ
せた後ホルムアルデヒド類を添加し塩基性触媒下でレゾ
ール化反応を進める桐油変性フェノール樹脂の製造に於
いて、レゾール化反応時にリン酸エステル化合物を添加
し、反応終点の高分子量物(≒4000)が反応生成
物中の20〜25重量%の範囲内になる様反応する事を
特徴とする熱硬化性樹脂の製造法。
1. A phosphoric acid ester at the time of resolization reaction in the production of tung oil-modified phenol resin in which phenols and tung oil are reacted under an acidic catalyst and then formaldehydes are added to proceed the resolization reaction under a basic catalyst. A process for producing a thermosetting resin, which comprises adding a compound and reacting so that a high molecular weight substance (≈4000) at the reaction end point is in the range of 20 to 25% by weight in the reaction product.
JP60034199A 1985-02-22 1985-02-22 Thermosetting resin manufacturing method Expired - Fee Related JPH0611779B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60034199A JPH0611779B2 (en) 1985-02-22 1985-02-22 Thermosetting resin manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60034199A JPH0611779B2 (en) 1985-02-22 1985-02-22 Thermosetting resin manufacturing method

Publications (2)

Publication Number Publication Date
JPS61192712A JPS61192712A (en) 1986-08-27
JPH0611779B2 true JPH0611779B2 (en) 1994-02-16

Family

ID=12407492

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60034199A Expired - Fee Related JPH0611779B2 (en) 1985-02-22 1985-02-22 Thermosetting resin manufacturing method

Country Status (1)

Country Link
JP (1) JPH0611779B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60255815A (en) * 1984-05-31 1985-12-17 Toshiba Chem Corp Production of flame-retarding phenolic resin composition

Also Published As

Publication number Publication date
JPS61192712A (en) 1986-08-27

Similar Documents

Publication Publication Date Title
JPH0665340A (en) Production of vegetable-oil-modified phenol resin for laminate
JPH0611779B2 (en) Thermosetting resin manufacturing method
US4229330A (en) Process for producing phenolic resins
JPS5831297B2 (en) Manufacturing method of phenolic resin laminate
JP3254792B2 (en) Production method of phenolic resin modified with vegetable oil
JPS61171717A (en) Production of oiticica oil-modified phenolic resin
JPS60192732A (en) Production of laminated sheet
JP3065383B2 (en) Manufacturing method of phenolic resin laminate
JPH0579092B2 (en)
JPS6051494B2 (en) Method for producing modified phenolic resin composition for flame-retardant laminates
KR820001054B1 (en) Process for producing phenolic resins
JPH0686511B2 (en) Method for producing oil-modified phenolic resin
JPS61171716A (en) Production of oiticica oil-modified phenolic resin
JPS61145216A (en) Production of water-soluble phenolic resin for laminate
JP3252730B2 (en) Method for producing phenolic resin composition
JPS6026489B2 (en) Production method of oil-modified phenolic resin for laminated products
JPH0542453B2 (en)
JPS61121932A (en) Manufacture of phenolic resin laminated sheet
JPS6250318A (en) Production of modified phenolic resin for laminated sheet
JPS6051493B2 (en) Method for producing phenolic resin composition for flame-retardant laminates
JPS62283117A (en) Production of oil-modified phenolic resin
JPH05320298A (en) Production of oil-modified phenolic resin for use in laminate
JPH0967420A (en) Production of resole-type phenolic resin composition
JPS5831298B2 (en) Manufacturing method of phenolic resin laminate
JPH0952927A (en) Production of phenol resin modified with diene polymer added with phenol

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees