JPS624720A - Novel resorcinol resin and its production - Google Patents

Novel resorcinol resin and its production

Info

Publication number
JPS624720A
JPS624720A JP14414785A JP14414785A JPS624720A JP S624720 A JPS624720 A JP S624720A JP 14414785 A JP14414785 A JP 14414785A JP 14414785 A JP14414785 A JP 14414785A JP S624720 A JPS624720 A JP S624720A
Authority
JP
Japan
Prior art keywords
dicyclopentadiene
resorcinol
resorcinol resin
catalyst
resin
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.)
Granted
Application number
JP14414785A
Other languages
Japanese (ja)
Other versions
JPH0674321B2 (en
Inventor
Hiroaki Nanba
宏彰 難波
Minoru Hishinuma
稔 菱沼
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.)
Sanyo Kokusaku Pulp Co Ltd
Original Assignee
Sanyo Kokusaku Pulp 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 Sanyo Kokusaku Pulp Co Ltd filed Critical Sanyo Kokusaku Pulp Co Ltd
Priority to JP14414785A priority Critical patent/JPH0674321B2/en
Publication of JPS624720A publication Critical patent/JPS624720A/en
Publication of JPH0674321B2 publication Critical patent/JPH0674321B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)

Abstract

PURPOSE:To produce the titled resin which can give a cured product having relaxed residual stress and flexibility, by polymerizing a resorcinol with dicyclopentadiene. CONSTITUTION:1mol of dicyclopentadiene and 0.5-20mol of a resorcinol are polymerized at 20-180 deg.C for several hr in the presence of a Lewis acid catalyst (e.g., AlCl3) and unreacted monomers are removed by vacuum distillation or fractional precipitation to obtain a resorcinol resin of the formula (wherein n is 0-15 on the average).

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は下記一般式〔1〕 〔式中、口は平均値O〜15を示す。〕で表わさ枕る新
規レゾルシノール樹脂及びその製造方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention is based on the following general formula [1] [wherein the value indicates an average value of 0 to 15]. This invention relates to a new resorcinol resin represented by the following formula and a method for producing the same.

〔従来の技術及び発明が解決しようとする問題点〕フェ
ノール樹脂及びレゾルシノール樹脂あるいは、レゾルシ
ノール変性フェノール樹脂は、機械的特性、電気的特性
、耐熱性、加工特性に優れているため電気・電子材料及
び塗料関係に広く使用されている。
[Prior art and problems to be solved by the invention] Phenol resins and resorcinol resins or resorcinol-modified phenol resins have excellent mechanical properties, electrical properties, heat resistance, and processing properties, so they are used in electrical and electronic materials and Widely used in paints.

最近、電子部品、中でも封止材料樹脂及び硬化剤に43
いでは、集積回路の高集積化に伴い、耐熱性の向上、硬
化後の残留応力の緩和が要求される一方、プリント配線
1.を盤用樹脂及び硬化剤では、耐熱性、可撓性の向上
が要求されている。
Recently, 43% has been applied to electronic parts, especially sealing material resins and hardening agents.
With the increase in the degree of integration of integrated circuits, improvements in heat resistance and relaxation of residual stress after curing are required. Resins and curing agents for discs are required to have improved heat resistance and flexibility.

従来、封止用樹脂材料において、硬化剤として用いられ
ているフェノールノボラックが硬化体に対して残留応力
緩和能、可撓性付与能が無いのに対し、それらをもつ硬
化剤を鋭意検討した。その結果、本発明の新規レゾルシ
ノール樹脂とぞの製造方法を見出した。
Phenol novolak, which has conventionally been used as a curing agent in resin materials for sealing, does not have the ability to relieve residual stress or impart flexibility to the cured product, so we have intensively investigated curing agents that have these properties. As a result, a method for producing the novel resorcinol resin of the present invention was discovered.

〔式中、0は前記に同じ。〕[In the formula, 0 is the same as above. ]

で表わされる新規レゾルシノール樹脂及びレゾルシノー
ル類とジシクロペンタジェンを触媒の存在下で重合させ
ることを特徴とする上記レゾルシノール樹脂の装造法に
関するものである。
The present invention relates to a novel resorcinol resin represented by the following formula and a method for preparing the resorcinol resin, which is characterized by polymerizing resorcinols and dicyclopentadiene in the presence of a catalyst.

従来のフェノールノボラック樹脂を硬化剤とした場合に
比べ、フェノールのかわりにレゾルシノールを用いるこ
とにより、水I1M当吊を上げ、硬化体の架橋密度を上
げることにより、耐熱性の向上をはかり、メチレンジヨ
イントのかわりに、ジシクロペンタジェンを用いること
により可撓性、応力緩和性をもたけることができる。
Compared to conventional phenol novolak resins used as curing agents, by using resorcinol instead of phenol, the water I1M capacity is increased and the crosslinking density of the cured product is increased, thereby improving heat resistance. By using dicyclopentadiene instead of Into, flexibility and stress relaxation properties can be imparted.

以下本発明を詳述する。The present invention will be explained in detail below.

本発明の新規レゾルシノール樹脂は、レゾルシノール類
とジシクロペンタジェンを触媒を用いて重合させること
により得られる。ここで使用されるレゾルシノール類と
は、レゾルシノール、2−メチルレゾルシノール等であ
るが、これにフェノール、クレゾール等のフェノール類
を混合し、共重合することも可能である。
The novel resorcinol resin of the present invention is obtained by polymerizing resorcinols and dicyclopentadiene using a catalyst. The resorcinols used here include resorcinol, 2-methylresorcinol, etc., but it is also possible to mix phenols such as phenol and cresol with these and copolymerize them.

触媒としては、ルイス酸であれば使用でき、AJ2C,
e3、BF5 、Zn CJ2z 、o−トルエンスル
ホン酸、r; c、e◆、H2SO4等を挙げることが
できる。
As a catalyst, any Lewis acid can be used, such as AJ2C,
Examples include e3, BF5, ZnCJ2z, o-toluenesulfonic acid, r;c, e♦, H2SO4, and the like.

触媒は単一あるいは、混合して使用することができる。A single catalyst or a mixture of catalysts can be used.

触媒の添加量は、ジシクロペンタジェン1モルに対しU
、  0.001〜0.1モル好ましくは、o、oos
〜0.05モルである。レゾルシノール類は、ジシクロ
ペンタジェン1モルに対し、0.5モル〜20モル、好
ましくは0.8〜8.0モルである。各物質の重合方法
としては、ジシクロペンタジェンとレゾルシノール類の
混合物に触媒を加えてもよいし、レゾルシノール類と触
媒の混合物にジシクロペンタジェンを加えてもよい。添
加時間は、配合によって異なるが、0.1へ・10時間
である。添加後反応系をさらに数時間反応させる。レゾ
ルシノール類とジシクロペンタジェンの重合反応温度は
、20〜180℃で好ましくは60〜120℃である。
The amount of catalyst added is U per mole of dicyclopentadiene.
, 0.001 to 0.1 mol, preferably o, oos
~0.05 mol. The amount of resorcinols is 0.5 to 20 mol, preferably 0.8 to 8.0 mol, per 1 mol of dicyclopentadiene. As a method for polymerizing each substance, a catalyst may be added to a mixture of dicyclopentadiene and resorcinols, or dicyclopentadiene may be added to a mixture of resorcinols and a catalyst. The addition time varies depending on the formulation, but is 0.1 to 10 hours. After the addition, the reaction system is allowed to react for several more hours. The polymerization reaction temperature of resorcinols and dicyclopentadiene is 20 to 180°C, preferably 60 to 120°C.

重合反応によって得られた樹脂は、用途によって、未反
応モノマーを除去する必要があり、また残存する触媒も
系外に取り出す必要がある。
Depending on the use of the resin obtained by the polymerization reaction, it is necessary to remove unreacted monomers, and it is also necessary to remove the remaining catalyst from the system.

未反応モノマーの除去法としては、減圧蒸留又は分別沈
澱が行えるが、またそれらを組み合わせた方法でもよい
。触媒の除去に関しては、BF3等では減圧蒸留により
モノマーと同口1に除去が可能であるが、AJICJI
!3その他の触媒除去においては、溶剤分離法によって
取り除くこともできる。
As a method for removing unreacted monomers, vacuum distillation or fractional precipitation can be used, but a combination of these methods may also be used. Regarding the removal of the catalyst, with BF3 etc., it is possible to remove it in the same volume as the monomer by vacuum distillation, but with AJICJI
! 3. Other catalysts can also be removed by a solvent separation method.

以F、減圧蒸留、分別沈澱、水洗等により不純物を取り
除いた後、減圧濃縮し一般式(I)で示される新規レゾ
ルシノール樹脂を得る。
Thereafter, impurities are removed by distillation under reduced pressure, fractional precipitation, washing with water, etc., and then concentrated under reduced pressure to obtain a new resorcinol resin represented by general formula (I).

〔実施例及び発明の効果〕[Examples and effects of the invention]

以下に実施例を挙げて説明するが、これらの実施例によ
って本発明は制限されるものではない。以下に部とある
のは、いずれも重量部である。
Examples will be described below, but the present invention is not limited to these Examples. All parts below are parts by weight.

実施例ル ゾルシノール      333部 ジシクロペンタジェン   138部 を、温度計、冷却器、撹拌装置、及び滴下管をイ1けた
反応器内に仕込み、80±5℃に保ち撹拌しながら、エ
チルエーテル50部に三フッ化ホウ素エーテル錯体(三
フッ化ホウ素47%)5部を溶解した液を2時間かけて
滴下した。
Example 333 parts of lusorcinol and 138 parts of dicyclopentadiene were placed in a reactor equipped with a thermometer, a condenser, a stirrer, and a dropping tube, and the mixture was added to 50 parts of ethyl ether while stirring while maintaining the temperature at 80±5°C. A solution containing 5 parts of boron trifluoride ether complex (47% boron trifluoride) was added dropwise over 2 hours.

反応液をさらに80±5°Cに2(時間保持、撹拌 4
した後、メタノール500部に溶解した。
The reaction solution was further heated to 80±5°C for 2 hours (maintained and stirred for 4 hours).
After that, it was dissolved in 500 parts of methanol.

メタノール溶液に水250部を加え、不溶解弁を回収し
、その中に残る溶媒を加熱留去し、目的とする重合物を
330部得た。
250 parts of water was added to the methanol solution, the insoluble valve was recovered, and the solvent remaining therein was distilled off under heating to obtain 330 parts of the desired polymer.

この重合物の特性を次の表−1及び添付の第1図ないし
第3図に示した。
The properties of this polymer are shown in the following Table 1 and the attached Figures 1 to 3.

表−1 1)GPC法による、ポリスチレン換綽値2)エタノー
ル溶液 カラム:TSK  GEL  4000HXLx1+3
000HXLx1+2000tlXLx2溶媒:TI−
IF、 1m、e/min 。
Table 1 1) Polystyrene conversion value by GPC method 2) Ethanol solution column: TSK GEL 4000HXLx1+3
000HXLx1+2000tlXLx2 Solvent: TI-
IF, 1m, e/min.

検出:R■ 3)日本電子製 Fx−900,溶媒量メタノールDetection: R■ 3) JEOL Fx-900, solvent amount methanol

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施例1化合物のGPC(ゲル・バー
ミコシ」ン・クロマトグラフ)を示す図表、第2図は同
一ヒのIRを示す図表、第3図は同一ヒのN M Rを
承り図表である。 (別  紙) 2、特許請求の範囲 1)下記一般式(I) 〔式中、nは平均値O〜15を示す。〕で表わされる新
規レゾルシノール樹脂。 2)レゾルシノール類とジシクロペンタジェンを触媒の
存在下で重合させることを特徴とする下記一般式(I)
で示される新規レゾルシノール樹脂の製造法。 (I)
Fig. 1 is a chart showing the GPC (gel vermicosin chromatography) of the compound of Example 1 of the present invention, Fig. 2 is a chart showing the IR of the same human, and Fig. 3 is a chart showing the NMR of the same human. This is an acceptance chart. (Attachment) 2. Claims 1) The following general formula (I) [wherein n represents an average value of 0 to 15]. ] A new resorcinol resin. 2) The following general formula (I), characterized in that resorcinols and dicyclopentadiene are polymerized in the presence of a catalyst.
A method for producing a new resorcinol resin shown in (I)

Claims (1)

【特許請求の範囲】 1)下記一般式〔 I 〕 ▲数式、化学式、表等があります▼ 〔 I 〕 〔式中、nは平均値0〜15を示す。〕 で表わされる新規レゾルシノール樹脂。 2)レゾルシノール類とジシクロペンタジエンを触媒の
存在下で重合させることを特徴とする下記一般式〔 I
〕で示される新規レゾルシノール樹脂の製造法。 ▲数式、化学式、表等があります▼ 〔 I 〕 〔式中、nは平均値0〜15を示す。〕
[Claims] 1) The following general formula [I] ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ [I] [In the formula, n indicates an average value of 0 to 15. ] A new resorcinol resin represented by 2) The following general formula [I] characterized by polymerizing resorcinols and dicyclopentadiene in the presence of a catalyst
] A method for producing a new resorcinol resin. ▲There are mathematical formulas, chemical formulas, tables, etc.▼ [I] [In the formula, n indicates an average value of 0 to 15. ]
JP14414785A 1985-07-01 1985-07-01 Novel resorcinol resin and method for producing the same Expired - Lifetime JPH0674321B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14414785A JPH0674321B2 (en) 1985-07-01 1985-07-01 Novel resorcinol resin and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14414785A JPH0674321B2 (en) 1985-07-01 1985-07-01 Novel resorcinol resin and method for producing the same

Publications (2)

Publication Number Publication Date
JPS624720A true JPS624720A (en) 1987-01-10
JPH0674321B2 JPH0674321B2 (en) 1994-09-21

Family

ID=15355307

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14414785A Expired - Lifetime JPH0674321B2 (en) 1985-07-01 1985-07-01 Novel resorcinol resin and method for producing the same

Country Status (1)

Country Link
JP (1) JPH0674321B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0798324A1 (en) * 1996-03-29 1997-10-01 Ceca S.A. Phenol-diene novolac resins, process for their preparation and rubber compositions containing said resins
US7135539B2 (en) 2000-09-08 2006-11-14 Schenectady International Inc. Novolac resins, process for preparing them and uses thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0798324A1 (en) * 1996-03-29 1997-10-01 Ceca S.A. Phenol-diene novolac resins, process for their preparation and rubber compositions containing said resins
FR2746803A1 (en) * 1996-03-29 1997-10-03 Ceca Sa PHENOL / DIENE NOVOLATE RESINS, PREPARATION METHOD AND RUBBER COMPOSITIONS COMPRISING SAID RESINS
US6265490B1 (en) 1996-03-29 2001-07-24 Ceca, S.A. Phenol/diene novolac resins, process of preparation and rubber-based compositions containing the said resins
US7135539B2 (en) 2000-09-08 2006-11-14 Schenectady International Inc. Novolac resins, process for preparing them and uses thereof

Also Published As

Publication number Publication date
JPH0674321B2 (en) 1994-09-21

Similar Documents

Publication Publication Date Title
US3106548A (en) Ethylenic polyamides
US4032513A (en) Process of producing alkenylphenol polymers
JPH0759619B2 (en) Method for producing high molecular weight epoxy resin
US3488332A (en) Process for preparation of living polymer
JPH0615609B2 (en) Process for producing poly (tetramethylene ether) glycol with narrow molecular weight distribution
JPS624720A (en) Novel resorcinol resin and its production
JPH07109331A (en) Production of high molecular weight epoxy resin
Matsuda Metal‐containing crosslinked polyester resins by combined polyesterification and polymerization of curable mixtures based on divalent metal salts of mono (hydroxyethyl) phthalate
EP0241133A2 (en) Polymaleimide compound and a composition containing the same
JPH01247402A (en) Chloroacetylated or alkylaminoacetylated styrene/isobutylene copolymer, production thereof, use of isobutylene for production of polyurethane or epoxy resin and use of isobutylene copolymer as crosslinkable polymer material
JP3054065B2 (en) Method for producing phenolic resin
JPS61145223A (en) Production of phenolic polymer
JPS627719A (en) Production of expoxy resin
US3260698A (en) Crystalline polyvinyl ethers prepared with chromic anhydride catalysts
JP2993727B2 (en) Method for producing phenolic polymer
US3385913A (en) Thermosetting copolymers based upon propylene oxide-butadiene monoxide copolymers
JPH0465430A (en) Fluorine-containing polysilethylene siloxane
JP3388880B2 (en) Isobutylene polymer and method for producing the same
JP4375824B2 (en) Method for producing high molecular weight epoxy polymer
JPH0129494B2 (en)
JP2899100B2 (en) Method for producing phenolic polymer
JPH0436161B2 (en)
JPS6392636A (en) Production of modified epoxy resin
Reardon et al. Preparation and Wetting Characteristics of Some Poly (fluorinated aromatic glycidyl ethers)
JPH04168122A (en) Production of phenol polymer

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term