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
JPS5948029B2 - Method for producing phenolic resin molding material - Google Patents
[go: Go Back, main page]

JPS5948029B2 - Method for producing phenolic resin molding material - Google Patents

Method for producing phenolic resin molding material

Info

Publication number
JPS5948029B2
JPS5948029B2 JP4328577A JP4328577A JPS5948029B2 JP S5948029 B2 JPS5948029 B2 JP S5948029B2 JP 4328577 A JP4328577 A JP 4328577A JP 4328577 A JP4328577 A JP 4328577A JP S5948029 B2 JPS5948029 B2 JP S5948029B2
Authority
JP
Japan
Prior art keywords
hexamine
molding material
phenolic resin
parts
resin molding
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
JP4328577A
Other languages
Japanese (ja)
Other versions
JPS53128655A (en
Inventor
拓二 伊藤
信作 浅尾
悦司 久保
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
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP4328577A priority Critical patent/JPS5948029B2/en
Publication of JPS53128655A publication Critical patent/JPS53128655A/en
Publication of JPS5948029B2 publication Critical patent/JPS5948029B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】 本発明はヘキサミンであらかじめ処理されたフィラーを
使用して、ロール、コニーダ等の乾式製造法で従来と同
じ方法で製造するフェノール樹脂成形材料の製造法で射
出成形法等で成形後の製品にボード等の内部欠陥の発生
しないフェノール樹脂成形材料の製造方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a method for producing a phenolic resin molding material using a filler pre-treated with hexamine and using a dry production method such as roll or co-kneader, which is the same as conventional methods, such as injection molding. The present invention relates to a method for producing a phenolic resin molding material that does not cause internal defects such as boards in the molded product.

フェノール樹脂成形材料より成形して得られる成形品の
品質は、使用するフェノール樹脂、基材滑剤等の種類及
び使用量の影響が大きく、これら組成と成形材料の流動
特性等で成形品の機械的、電気的等の特性が決まる。し
かしながら、成形品形状、金型構造、及びその他成形条
件等のにより、同じフェノール成形材料でも同じ特性が
得られないことが多い。この原因として基材の配向等、
組成的原因もあるが、成形品中のボード等の内部欠陥も
原因となつている。すなわち、ボード等の内部欠陥は強
度のバラツキを生じやすく、かつ電気的特性でも耐電圧
等の著しい低下を生ずることがある。本発明はこれら成
形品特性のバラツキの原因となるボード等の内部欠陥の
生じない、フェノール樹脂成形材料の製造方法に関する
ものである。
The quality of molded products obtained by molding from phenolic resin molding materials is greatly influenced by the types and amounts of the phenolic resins and base lubricants used, and the mechanical properties of the molded products are affected by these compositions and the flow characteristics of the molding materials. , electrical characteristics etc. are determined. However, depending on the shape of the molded product, mold structure, and other molding conditions, it is often not possible to obtain the same properties even with the same phenolic molding material. This may be due to the orientation of the base material, etc.
There are compositional causes, but internal defects in the boards in the molded product are also causes. That is, internal defects in the board or the like tend to cause variations in strength, and may also cause a significant decrease in electrical properties such as withstand voltage. The present invention relates to a method for producing a phenolic resin molding material that does not cause internal defects such as boards that cause variations in the properties of these molded products.

本発明は前記特性のバラツキの原因となる成形品内部の
欠陥を解消せんとするもので、ヘキサミンをあらかじめ
基材に処理した後、従来の方法でフェノール成形材料を
製造する方法である。以下本発明について詳細に説明す
る。フェノール樹脂成形材料の製造法には、ノボラック
樹脂を使用しヘキサミンで硬化させる二段法と、レゾー
ル樹脂を使用する一段法があり、また、樹脂等を溶剤に
溶かしニーダ等で混練しさらに乾燥する湿式法と、原材
料をブレンターまたはペンシェルミキサー等で均一に混
合し、これをさらにロール、コニーダ等で捏和する乾式
法があるが、本発明はヘキサミンを硬化剤として使用す
る二段法でかつ乾式法に著しい効果がある。
The present invention aims to eliminate the defects inside the molded product that cause the above-mentioned variations in properties, and is a method for producing a phenol molding material by a conventional method after treating a base material with hexamine in advance. The present invention will be explained in detail below. There are two methods for manufacturing phenolic resin molding materials: a two-step method using novolak resin and curing with hexamine, and a one-step method using resol resin.Also, there are two methods for producing phenolic resin molding materials: a two-step method using novolac resin and curing with hexamine, and a one-step method using resol resin. There is a wet method and a dry method in which raw materials are uniformly mixed with a blender or pen shell mixer, etc., and then kneaded with a roll, co-kneader, etc., but the present invention is a two-step method using hexamine as a hardening agent. The dry method has remarkable effects.

処理とは1ヘキサミンを溶剤に溶解し2フィラーと均一
に混合し3溶剤を乾燥し、ヘキサミンが付着したフィラ
ーを粉体として取扱い得る状態にすることをいう。
Processing refers to dissolving 1 hexamine in a solvent, mixing it uniformly with 2 filler, drying the solvent 3, and making the filler to which hexamine is attached into a state in which it can be handled as a powder.

ヘキサミンを溶解する溶剤には水、メタノール、クロロ
ホルム等があるが、溶解度等の点で水が最もすぐれてい
る。
Solvents for dissolving hexamine include water, methanol, and chloroform, but water is the best in terms of solubility.

ヘキサミンを水に溶かしたヘキサ水の濃度は溶解度より
約48%が上限である。
The upper limit of the concentration of hexawater in which hexamine is dissolved in water is about 48% based on the solubility.

それ故45%以上ではヘキサミンの析出が生ずることが
あり、このように析出した場合ヘキサミンの大きな結晶
を生成するので濃度の上限は45%が適当である。次に
濃度の下限については低濃度ほどヘキサミンの析出およ
びフィラ一との均一な混合が出来るが、水が多過ぎると
、混合後放置すると上層から下層への移行が生じ、不均
一となつたり、また、乾燥しにくくなる。それ故下限の
濃度は30%が適当であり一般的には40%が最適であ
る。ヘキサ水とフイラ一との混合は、ニーダ一、ペンシ
ェルミキサ等の従来の湿式混合機を用い、これにあらか
じめフイラ一を入れておき、撹拌しながらヘキサ水を投
入して行う。フイラ一を処理するヘキサミン量は、最終
組成で使用するヘキサミン量の全量をフイラ一に処理す
る。
Therefore, if the concentration exceeds 45%, precipitation of hexamine may occur, and if such precipitation occurs, large crystals of hexamine will be formed, so an appropriate upper limit of the concentration is 45%. Next, regarding the lower limit of the concentration, the lower the concentration, the more the hexamine can be precipitated and the more uniformly mixed with the filler, but if there is too much water and left to stand after mixing, it will migrate from the upper layer to the lower layer, resulting in non-uniformity. It also becomes difficult to dry. Therefore, a suitable lower limit concentration is 30%, and generally 40% is optimal. The hexa water and the filler are mixed using a conventional wet mixer such as a kneader or a pen shell mixer, the filler is placed in advance, and the hexa water is added while stirring. The amount of hexamine used in the filler is equal to the total amount of hexamine used in the final composition.

ヘキサ水で処理した基材は100℃以下で乾燥し、含水
量5〜15(F6に調整し、これを従来法と同様に、ブ
レンダ一、ペンシェルミキサー等で混合しさらにロール
、コニーダ等で捏和し成形材料とする。
The base material treated with hexa water is dried at below 100°C, and the moisture content is adjusted to 5 to 15 (F6). As in the conventional method, this is mixed using a blender, a pen shell mixer, etc., and then a roll, co-kneader, etc. Knead and use as a molding material.

含水量が15%以上だと部分的なプロツクなどがおこり
均一な混合が困難となり、又5(fl)以下だとロール
捏和等が困難となり成形材料の流動性が悪くなる。フイ
ラ一には木粉 パルプ等の有機質フイラ一とアスベスト
、炭酸カルシウム、クレー等の無機質フイラ一があるが
、本発明はこれらすべてのフイラ一について適用できる
If the water content is more than 15%, partial blockage will occur and uniform mixing will be difficult, while if it is less than 5 (fl), roll kneading etc. will be difficult and the fluidity of the molding material will be poor. Fillers include organic fillers such as wood flour and pulp, and inorganic fillers such as asbestos, calcium carbonate, clay, etc., and the present invention is applicable to all of these fillers.

また、消石灰、酸化マグネシウム、酸化亜鉛等のアルカ
リ土類金属化合物、顔料、離型剤、フルフラール等の可
塑剤等が使用されることが、本発明は従来の組成がその
まま適用できるものである。
In addition, alkaline earth metal compounds such as slaked lime, magnesium oxide, and zinc oxide, pigments, mold release agents, and plasticizers such as furfural are used, and conventional compositions can be applied to the present invention as they are.

以下、本発明の実施例に基づいて具体的に説明する。Hereinafter, the present invention will be specifically explained based on examples.

実施例 1 ヘキサミン6.3部を水12.6部に溶解しヘキサ水を
作成する。
Example 1 Hexawater was prepared by dissolving 6.3 parts of hexamine in 12.6 parts of water.

次に木粉36.2部にヘキサ水18.9部を加え、ペン
シェルミキサーで10分間混合し、これを80℃で1時
間乾燥しヘキサ処理木粉を得た。上記ヘキサ処理木粉を
ペンシェルミキサに入れ、これにノボラツク樹脂42部
、消石灰1部、ステアリン酸亜鉛1.5部、顔料2部、
フルフラール2部、アスベスト6部を加え10分間混合
し均一な混合粉を得る。次にこの混合粉を前ロール90
℃、後ロール80℃のロール温度で5分間混合し、さら
に粉砕して成形材料を得た。実施例 2 木粉100部をヘキサミン40(F6の水溶液57部を
加え二ーダで30分間混合し、均一にする。
Next, 18.9 parts of hexa water was added to 36.2 parts of wood flour, mixed for 10 minutes using a pen shell mixer, and dried at 80° C. for 1 hour to obtain hexa-treated wood flour. Put the above-mentioned hexa-treated wood flour into a pen shell mixer, add 42 parts of novolac resin, 1 part of slaked lime, 1.5 parts of zinc stearate, 2 parts of pigment,
Add 2 parts of furfural and 6 parts of asbestos and mix for 10 minutes to obtain a uniform mixed powder. Next, apply this mixed powder to the front roll 90
The mixture was mixed for 5 minutes at a roll temperature of 80° C. and a rear roll for 5 minutes, and further pulverized to obtain a molding material. Example 2 57 parts of an aqueous solution of Hexamine 40 (F6) was added to 100 parts of wood flour and mixed in a kneader for 30 minutes to make the mixture uniform.

これを80℃で処理物の含水率10%になるまで乾燥し
ヘキサミン処理木粉を得た。次に上記ヘキサミン処理木
粉45.5部、ノボラツク樹脂42部、消石灰1部、顔
料2部、フルフラール2部、炭酸カルシウム6部をブレ
ンダ一で30分間均一に混合し、さらに前ロール90℃
、後ロール80℃のロール温度で5分間で捏和し得られ
たシートを粉砕し成形材料を得た。
This was dried at 80° C. until the moisture content of the treated material was 10% to obtain hexamine-treated wood flour. Next, 45.5 parts of the above hexamine-treated wood flour, 42 parts of novolak resin, 1 part of slaked lime, 2 parts of pigment, 2 parts of furfural, and 6 parts of calcium carbonate were uniformly mixed in a blender for 30 minutes, and then the front roll was heated to 90°C.
The resulting sheet was kneaded for 5 minutes at a rear roll temperature of 80° C. and the resulting sheet was pulverized to obtain a molding material.

比較例 実施例1の配合割合でヘキサミンをヘキサ水として木粉
に処理しないでペンシェルミキサーで10分間均一に混
合し、さらに同様にロール粉砕して成形材料を得た。
Comparative Example Hexawater was mixed with hexamine at the mixing ratio of Example 1, without being processed into wood flour, and mixed uniformly for 10 minutes in a pen shell mixer, followed by roll pulverization in the same manner to obtain a molding material.

以上の実施例1,2、および比較例の成形材料を射出成
形機RJ−75A(名機製作所製)でシリンダ温度、前
部90℃、後部70℃、金型温度180℃で射出圧50
k9/CflGで157!Tm角の棒状成形品、47!
171L厚さの板を成形し、これを切断し、内部のボー
ドの有無を調べた。
The molding materials of Examples 1 and 2 and Comparative Examples above were molded using an injection molding machine RJ-75A (manufactured by Meiki Seisakusho) at a cylinder temperature of 90°C at the front, 70°C at the rear, and an injection pressure of 50°C at a mold temperature of 180°C.
157 with k9/CflG! Tm square rod-shaped molded product, 47!
A plate with a thickness of 171L was formed, cut, and the presence or absence of the board inside was examined.

成形品をダイャモンドカツタ一等で切断しかつサンドペ
ーパ(#800〜#1500)で研摩した後、目視また
は顕微鏡等で倍率60〜600でボードの大きさを判定
した。
After cutting the molded product with a diamond cutter of the first grade and polishing it with sandpaper (#800 to #1500), the size of the board was determined visually or with a microscope at a magnification of 60 to 600.

その結果を下に示す。追加比較例比較例と同一配合で樹
脂以外とメタノール10部を100℃に加熱したペンシ
ェルミキサーに投入し、5分間混合した後、冷却する。
The results are shown below. Additional Comparative Example The same composition as in the comparative example except for the resin and 10 parts of methanol were placed in a pen shell mixer heated to 100°C, mixed for 5 minutes, and then cooled.

この混合物にあらかじめ微粉砕したノボラツク樹脂を添
加混合し、90〜110℃の加熱ロールで1.5分間混
練し、冷却後粉砕してフエノール樹脂成形材料を得た。
比較例 個数3〜6個/cm2 最大直径約0.1mm。
A novolak resin that had been finely ground in advance was added to this mixture, kneaded for 1.5 minutes with heated rolls at 90 to 110°C, cooled, and then ground to obtain a phenolic resin molding material.
Comparative example Number of pieces: 3 to 6 pieces/cm2 Maximum diameter: about 0.1 mm.

Claims (1)

【特許請求の範囲】[Claims] 1 ヘキサミンを溶剤に溶解しフィラーと均一に混合し
た後、溶剤を乾燥して得られるヘキサミンが付着した粉
体状のフィラーを使用することを特徴とするフェノール
樹脂成形材料の製造方法。
1. A method for producing a phenolic resin molding material, which uses a powdered filler to which hexamine is obtained by dissolving hexamine in a solvent, uniformly mixing it with the filler, and then drying the solvent.
JP4328577A 1977-04-14 1977-04-14 Method for producing phenolic resin molding material Expired JPS5948029B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4328577A JPS5948029B2 (en) 1977-04-14 1977-04-14 Method for producing phenolic resin molding material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4328577A JPS5948029B2 (en) 1977-04-14 1977-04-14 Method for producing phenolic resin molding material

Publications (2)

Publication Number Publication Date
JPS53128655A JPS53128655A (en) 1978-11-09
JPS5948029B2 true JPS5948029B2 (en) 1984-11-22

Family

ID=12659523

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4328577A Expired JPS5948029B2 (en) 1977-04-14 1977-04-14 Method for producing phenolic resin molding material

Country Status (1)

Country Link
JP (1) JPS5948029B2 (en)

Also Published As

Publication number Publication date
JPS53128655A (en) 1978-11-09

Similar Documents

Publication Publication Date Title
US2168160A (en) Production of phenol-aldehydelignin resins
JP2000026141A (en) Carbon black for coloring cement and method for coloring cement molded articles
US4194996A (en) Phenol formaldehyde compression moulding composition comprising phenol formaldehyde-wood filler
JPS5948029B2 (en) Method for producing phenolic resin molding material
CN107216669B (en) Simultaneous recycling method of phenolic resin and biochemical sludge in phenolic resin production wastewater treatment
JPS5948028B2 (en) Method for producing phenolic resin molding material
US1609506A (en) Method of plasticizing phenolic molding materials
RU2100129C1 (en) Method of treating low-grade bentonites
US4195019A (en) Wood and phenol-formaldehyde compression-moulding composition and method for preparing the same
US1952041A (en) Rubber goods and method of manufacturing the same
SU1692998A1 (en) Polymeric moulding composition
US1339134A (en) Phenolic comdensation product and procres of manufacturing
JP2930819B2 (en) Method for producing phenolic resin molding material
DE2927053A1 (en) Old paper and thermoplastic resin-contg. composite material prodn. - by comminuting paper, mixing with resin and drying, melting, kneading and granulating
SU709380A1 (en) Method of obtaining compositions for impact-resistant materials
JPS6054971B2 (en) Manufacturing method of phenolic resin molding material
JPH11246285A (en) Hard wood chip cement molding
SU531828A1 (en) Polymer Press Position
JPS6086060A (en) Manufacture of excelsior cement board
US1146299A (en) Plastic molding composition and method of producing same.
KR930011523B1 (en) Manufacturing method of organic binder for casting
JPS637939A (en) Preparation of matrix for plate making
JPS61229510A (en) Manufacture of rubber-inorganic fiber composition
KR790001272B1 (en) Method of manufacture for light material of building
JPS6086061A (en) Manufacture of excelsior cement board