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
JPS6034567B2 - Manufacturing method of phenolic resin - Google Patents
[go: Go Back, main page]

JPS6034567B2 - Manufacturing method of phenolic resin - Google Patents

Manufacturing method of phenolic resin

Info

Publication number
JPS6034567B2
JPS6034567B2 JP5204478A JP5204478A JPS6034567B2 JP S6034567 B2 JPS6034567 B2 JP S6034567B2 JP 5204478 A JP5204478 A JP 5204478A JP 5204478 A JP5204478 A JP 5204478A JP S6034567 B2 JPS6034567 B2 JP S6034567B2
Authority
JP
Japan
Prior art keywords
resin
phenol
phenolic resin
acid
phosphoric acids
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
Application number
JP5204478A
Other languages
Japanese (ja)
Other versions
JPS54143492A (en
Inventor
隆 紺谷
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP5204478A priority Critical patent/JPS6034567B2/en
Publication of JPS54143492A publication Critical patent/JPS54143492A/en
Publication of JPS6034567B2 publication Critical patent/JPS6034567B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Phenolic Resins Or Amino Resins (AREA)

Description

【発明の詳細な説明】 本発明は、主としてフェノール樹脂の製法に関するもの
であり、禾反応フェノールが少なく、成形収縮の少ない
フェノール樹脂を得ることを目的とするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention mainly relates to a method for producing a phenol resin, and its object is to obtain a phenol resin that contains less reaction phenol and has less mold shrinkage.

従来、成形材料に用いられるフェノール樹脂はフェノー
ル類とホルムアルデヒドを酸触媒として修酸または塩酸
等をモル比が0.5〜1.0で合成して得られるもので
あるが、この樹脂中には通常5〜10%の未反応フェノ
−ルが含まれる。
Conventionally, phenolic resins used as molding materials are obtained by synthesizing oxalic acid or hydrochloric acid using phenols and formaldehyde as acid catalysts at a molar ratio of 0.5 to 1.0. It usually contains 5-10% unreacted phenol.

得られたフェノール樹脂を用いて成形材料化して成形し
た場合に、成形収縮が大きい欠点があった。
When the obtained phenolic resin is used as a molding material and molded, there is a drawback that molding shrinkage is large.

又成形後、経時変化における収縮も大きい。これは、成
形品中に残存する未反応フェノールが経時的に揮発する
ためと思われる。又成形材料の製造の際及び成形の際に
もフェノールの揮発が生じ、有毒の臭いを発生するため
、作業環境の面からも未反応分の少ないフェノールが望
まれていた。近年、この問題を鱗決すべく、薄膜乾燥な
どの工法により未反応フェノールの少ない樹脂の合成法
が考案されたが、揮発したフェノールの回収が困難な事
から樹脂のコスト上昇を招く恐れがあつた。本発明は上
記欠点に鑑みてなされたものであり、未反応フェノール
が少なく、成形収縮の少ないフェノール樹脂の製法を提
供するものである。
Furthermore, after molding, there is a large amount of shrinkage over time. This seems to be because unreacted phenol remaining in the molded article volatilizes over time. In addition, phenol volatilizes during the production and molding of molding materials and generates a toxic odor, so phenol with less unreacted content has been desired from the viewpoint of the working environment. In recent years, in order to solve this problem, methods for synthesizing resins with less unreacted phenol using methods such as thin film drying have been devised, but this may lead to an increase in the cost of the resin because it is difficult to recover the volatilized phenol. . The present invention has been made in view of the above-mentioned drawbacks, and it is an object of the present invention to provide a method for producing a phenolic resin with less unreacted phenol and less molding shrinkage.

しかして本発明は、フェノール類とホルムアルデヒドを
反応せしめてフェノール樹脂を合成する場合において、
触媒としてリン酸類をフェノール類1モルに対して少な
くとも0.01モル以上を添加して樹脂を合成後、ホゥ
酸をリン酸類の1.3音量モル加えて中和することを特
徴とする。以下、本発明を詳細に説明する。本発明はフ
ェノール類とホルムアルデヒドを触媒を用いて合成する
ノボラック型フェノール樹脂の製法である。
However, in the present invention, when a phenol resin is synthesized by reacting phenols with formaldehyde,
The method is characterized in that the resin is synthesized by adding at least 0.01 mole or more of phosphoric acids per mole of phenol as a catalyst, and then neutralizing by adding boric acid to 1.3 volume moles of the phosphoric acids. The present invention will be explained in detail below. The present invention is a method for producing a novolac type phenolic resin by synthesizing phenols and formaldehyde using a catalyst.

ここでいうフェノール類とは、フェノール、クレゾール
、ノニルフエノール、クロルフエノールなどである。ホ
ルムアルデヒドは37%ホルムアルデヒド、50%ホル
ムアルデヒド、パルホルムホルムアルデヒドなどをいう
。このフェノール類とホルムアルデヒドを0.5〜1.
0のモル比で配合し、リン酸類を触媒として縮合反応を
行なってフェノール樹脂を得る方法である。リン酸類と
しては5酸化2リンを水和してできる。オルトリン酸、
メタリン酸、亜リン酸、次亜リン酸などが用いられ、フ
ェノ−ル類1モルに対して少なくとも0.01モル以上
添加して用いるのが好ましい。これはリン酸類が少ない
と未反応フェノールが比較的多く残存するためであり、
最も好ましくは0.01〜0.05モルの範囲である。
これはリン酸類が0.05モルを超えても、未反応フェ
ノール分が一定量となり、それ以上の効果を得にくいた
めである。このリン酸類は単独でいたほうが未反応分の
少ないものが得られるが他の酸触媒、例えば修酸または
塩酸などを併用して用いてもよい。又、リン酸類と併用
して2価、3価の金属塩(酢酸亜鉛またはホウ酸マンガ
ンなど)を用いてフェノール樹脂のo/p比を高め、反
応速度をはやめて反応を行っても同様に未反応フェノー
ルの少ないものが得られる。このようにして合成される
フェノール樹脂を、脱水時に120℃以上の温度で30
分以上加熱しながらホゥ酸またはメタホゥ酸をリン酸類
の1.5倍量モル加えて、残余のリン酸類を中和する。
The phenols mentioned here include phenol, cresol, nonylphenol, chlorphenol, and the like. Formaldehyde refers to 37% formaldehyde, 50% formaldehyde, parformaldehyde, etc. This phenol and formaldehyde are mixed in a proportion of 0.5 to 1.
In this method, a phenolic resin is obtained by blending the resins in a molar ratio of 0 and carrying out a condensation reaction using phosphoric acids as a catalyst. Phosphoric acids are produced by hydrating diphosphorus pentoxide. orthophosphoric acid,
Metaphosphoric acid, phosphorous acid, hypophosphorous acid, etc. are used, and it is preferable to use them in an amount of at least 0.01 mol or more per 1 mol of phenols. This is because when phosphoric acids are low, a relatively large amount of unreacted phenol remains.
The most preferred range is 0.01 to 0.05 mol.
This is because even if the amount of phosphoric acids exceeds 0.05 mol, the amount of unreacted phenol remains at a certain level, making it difficult to obtain further effects. When these phosphoric acids are used alone, less unreacted components can be obtained, but other acid catalysts such as oxalic acid or hydrochloric acid may be used in combination. In addition, the same effect can be obtained even if the reaction is carried out by increasing the O/P ratio of the phenol resin by using divalent or trivalent metal salts (such as zinc acetate or manganese borate) in combination with phosphoric acids and slowing down the reaction rate. A product containing less unreacted phenol can be obtained. The phenolic resin synthesized in this way is heated to 30°C at a temperature of 120°C or higher during dehydration.
Boric acid or metaboric acid is added in a molar amount 1.5 times the amount of phosphoric acids while heating for at least 1 minute to neutralize the remaining phosphoric acids.

リン酸類の中和にアルカリを用いた場合は、中和後、塩
が析出するため不適当である。上記したように本発明は
、フェノール類とホルムァルデヒドを反応せしめてフェ
ノール樹脂を合成する場合において、触媒としてリン酸
類をフェノール類1モルに対して少なくとも0.01モ
ル以上を添加して樹脂を合成後、ホウ酸をリン酸類の1
.牙音量モル加えて中和することを特徴とするので、得
られたフェノール樹脂は、未反応フェノール分が少なく
、貯蔵時のケーキングを生じ‘こくいのであり、その製
造に際しては、廃液中にフェノール量が少ないため廃液
処理が簡単で、しかも樹脂の収率が高い利点を有し、こ
の樹脂を用いても得られた成形材料は成形収縮が小さく
、かつ経時の寸法変化も小さく熱的強度の優れたものが
得られる。
When an alkali is used to neutralize phosphoric acids, it is unsuitable because salts precipitate after neutralization. As described above, in the case of synthesizing a phenol resin by reacting phenols with formaldehyde, the present invention adds at least 0.01 mole or more of phosphoric acid as a catalyst to 1 mole of phenol to synthesize the resin. After synthesis, boric acid is converted into one of the phosphoric acids.
.. Since the phenol resin obtained has a small amount of unreacted phenol, it is difficult to cause caking during storage. Since the amount is small, waste liquid treatment is easy, and it has the advantage of high resin yield. Even when using this resin, the molding material obtained has small mold shrinkage and dimensional change over time, and has low thermal strength. You can get something excellent.

以下、本発明の示施例を示す。Examples of the present invention are shown below.

実施例 1〜6 第1表の配合で混合して、還流温度で3時間反応させて
、更にホウ酸をリン酸類の1.5倍量モル加えて煮詰め
時120oo、30分以上加熱して中和反応を行い、フ
ェノール樹脂を得た。
Examples 1 to 6 Mix the ingredients in Table 1, react at reflux temperature for 3 hours, add boric acid in an amount 1.5 times the mole of phosphoric acids, boil down to 120 oo, and heat for 30 minutes or more. A phenol resin was obtained by a sum reaction.

比較例 第1表の配合で実施例と同様にして還流温度で3時間反
応させて、フェノール樹脂を得た。
Comparative Example A phenol resin was obtained by reacting at reflux temperature for 3 hours using the formulation shown in Table 1 in the same manner as in the example.

第1表各実施例及び比較例で得られたフェノール樹脂の
物性をそれぞれ測定してその結果を第2表に示す。
Table 1 The physical properties of the phenolic resins obtained in each Example and Comparative Example were measured and the results are shown in Table 2.

ここで未反応フェノールはブロム化法により行い、数平
均分子量はGPCにより算出し、レジン粘度はB型粘度
計にて16000で測定し、レジンpHは樹脂5夕をメ
タノール10夕で溶解後、水45夕を添加し上燈液をp
Hメーターにて測定し、軟化点は環球法により測定した
。第2表
Here, unreacted phenol was removed by the bromination method, the number average molecular weight was calculated by GPC, the resin viscosity was measured at 16,000 using a B-type viscometer, and the resin pH was determined by dissolving 5 parts of the resin in 10 parts of methanol, then water. Add 45 yen and add top solution.
It was measured with an H meter, and the softening point was measured by the ring and ball method. Table 2

Claims (1)

【特許請求の範囲】[Claims] 1 フエノール類とホルムアルデヒドを反応せしめてフ
エノール樹脂を合成する場合において、触媒としてリン
酸類をフエノール類1モルに対して少なくとも0.01
モル以上を添加して樹脂を合成後、ホウ酸をリン酸類の
1.5倍量モル加えて中和することを特徴とするフエノ
ール樹脂の製法。
1. When synthesizing phenolic resin by reacting phenols and formaldehyde, use at least 0.01 phosphoric acid as a catalyst per mole of phenols.
A method for producing a phenolic resin, which comprises adding boric acid in an amount 1.5 times the amount of phosphoric acid to neutralize the resin after synthesizing the resin.
JP5204478A 1978-04-28 1978-04-28 Manufacturing method of phenolic resin Expired JPS6034567B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5204478A JPS6034567B2 (en) 1978-04-28 1978-04-28 Manufacturing method of phenolic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5204478A JPS6034567B2 (en) 1978-04-28 1978-04-28 Manufacturing method of phenolic resin

Publications (2)

Publication Number Publication Date
JPS54143492A JPS54143492A (en) 1979-11-08
JPS6034567B2 true JPS6034567B2 (en) 1985-08-09

Family

ID=12903808

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5204478A Expired JPS6034567B2 (en) 1978-04-28 1978-04-28 Manufacturing method of phenolic resin

Country Status (1)

Country Link
JP (1) JPS6034567B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5876976B2 (en) * 2009-01-09 2016-03-02 アイカSdkフェノール株式会社 Novolac resin and thermosetting resin composition

Also Published As

Publication number Publication date
JPS54143492A (en) 1979-11-08

Similar Documents

Publication Publication Date Title
JPS6034567B2 (en) Manufacturing method of phenolic resin
US2168981A (en) Phenolic resin molding composition
CA1196022A (en) Hemi-formals of methylolated phenols
US4094825A (en) Process for the production of phenol silicoformate compounds and their condensation products
US4299947A (en) Process for producing quick-curing phenolic resin
US2497073A (en) Reaction products of dicyandiamide with an amine-formaldehyde reaction product
US3324082A (en) Ureidomethyl diaromatic etheraldehyde polymers
US2056454A (en) Molding powders and method of molding them
JPH032169B2 (en)
JP4206909B2 (en) Method for producing triazine-modified novolac-type phenolic resin
SU392712A1 (en)
JPS6115085B2 (en)
US3123586A (en) Glycidyl ethers of mononuclear poly-
JPS62230815A (en) Quick-curing novolak type phenolic resin and production thereof
US2868747A (en) Furan resin compositions including tall oil and an aromatic aldehyde
JPH03103417A (en) Production of self-curing phenolic resin
JPH03111416A (en) Preparation of self-curable phenolic resin
KR100561898B1 (en) High Molecular Weight High Ortho Novolac Phenolic Resin
JPS5948049B2 (en) Method for producing fast-curing phenolic resin
JPS5817529B2 (en) Manufacturing method of novolak resin
JP3062211B2 (en) Method for producing self-curing phenolic resin
JPH04149222A (en) Production of phenolic resin
JPH0670114B2 (en) Method for producing self-curing phenolic resin
US3950309A (en) Novel thermosetting resins and process for preparing the same comprising reacting a novolak with a titanic acid ester
JPS5829971B2 (en) Method for producing phenolic resin molding material