JPS5825571B2 - Netsukou Kaseiji Yushisei Keizai Ryouno Seizouhouhou - Google Patents
Netsukou Kaseiji Yushisei Keizai Ryouno SeizouhouhouInfo
- Publication number
- JPS5825571B2 JPS5825571B2 JP12802775A JP12802775A JPS5825571B2 JP S5825571 B2 JPS5825571 B2 JP S5825571B2 JP 12802775 A JP12802775 A JP 12802775A JP 12802775 A JP12802775 A JP 12802775A JP S5825571 B2 JPS5825571 B2 JP S5825571B2
- Authority
- JP
- Japan
- Prior art keywords
- molding
- molding material
- yushisei
- seizouhouhou
- ryouno
- 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
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Glanulating (AREA)
Description
【発明の詳細な説明】
本発明は熱硬化性樹脂成形材料の製造方法に関するもの
で、射出成形機ホッパーからシリンダー内に安定して材
料を供給できる球状の成形材料の製造方法を提供するこ
とにある。Detailed Description of the Invention The present invention relates to a method for producing a thermosetting resin molding material, and an object of the present invention is to provide a method for producing a spherical molding material that can stably supply the material from an injection molding machine hopper into a cylinder. be.
現在、一般的な熱硬化性樹脂用射出成形機である、イン
ライン型射出成形機で安定して成形できる熱硬化性樹脂
成形材料には、フェノール樹脂成形材料、アルキド樹脂
成形材料、ジアリルフタレート樹脂成形材料などがある
。Currently, thermosetting resin molding materials that can be stably molded using in-line injection molding machines, which are common injection molding machines for thermosetting resins, include phenolic resin molding materials, alkyd resin molding materials, and diallyl phthalate resin molding materials. There are materials etc.
インライン型射出成形機で安定して連続成形するには、
シリンダ内で安定であるとともに、射出成形機のホッパ
からシリンダ内に材料が安定して供給できることが必要
である。To perform stable continuous molding with an inline injection molding machine,
It is necessary that the material is stable within the cylinder and that the material can be stably supplied into the cylinder from the hopper of the injection molding machine.
そのため成形材料の形状は一般的には一定粒度の粉状で
ある。Therefore, the shape of the molding material is generally a powder with a constant particle size.
非成形材料の取扱い、およびシリンダ内へのバラツキの
ない供給性を得るためには微粉が少く粒度分布の小さい
ことが望ましく材料の形状としては一定の粒度の球状が
最適である。In order to handle the non-molded material and to obtain uniform supply into the cylinder, it is desirable that the material has a small amount of fine powder and a small particle size distribution, and the optimal shape of the material is a spherical shape with a constant particle size.
材料を一定形状にする造粒方法には、押出機を使用する
方法や、ヘンシェルミキサー等の高速攪拌機を使用して
造粒する方法など種々あるが、いずれも配合組成が限定
される。There are various granulation methods for forming materials into a certain shape, such as a method using an extruder and a method of granulation using a high-speed stirrer such as a Henschel mixer, but each method has a limited composition.
また、ハンマーミルなどによる粉砕法で、は、充てん剤
にビニロン、ガラス繊維、アスベスト繊維などの長繊維
を使用すると成形材料のカサバリが大きくなり、ホッパ
ーからシリンダ内に安定した材料の供給できなく連続射
出成形が不可能となる。In addition, when using a crushing method using a hammer mill, etc., if long fibers such as vinylon, glass fiber, or asbestos fiber are used as a filler, the bulk of the molding material increases, making it impossible to stably supply the material from the hopper into the cylinder. Injection molding becomes impossible.
また、粉砕により繊維の切断、分離が激しく強度が低下
する原因となる。In addition, pulverization causes severe cutting and separation of fibers, which causes a decrease in strength.
また、低軟化点の樹脂を使用した成形材料では、粉砕機
の摩擦熱により、粉砕は困難である。Furthermore, it is difficult to crush a molding material using a resin with a low softening point due to the frictional heat of the crusher.
本発明は、従来の欠点を解消しいかなる配合組成の材料
であっても安定して連続成形ができる、球状の成形材料
の製造方法を提供することを目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a spherical molding material, which eliminates the conventional drawbacks and allows stable and continuous molding of materials of any composition.
本発明は成形材料配合組成物をニーダ、ロールなどで混
和し均一な組成物を作成し、これをシート化したのち切
断しベレットを作る。In the present invention, a molding material composition is mixed with a kneader, a roll, etc. to create a uniform composition, which is formed into a sheet and then cut to make a pellet.
このベレットに粒径0.2μ以下、融点90℃以上の微
粉末をベレットに対し、0.2〜1.0重量%添加し、
ヘンシェルミキサなどの高速攪拌機で1000〜300
0 pmで5〜10分間攪拌し球状の成形材料を得る方
法である。To this pellet, 0.2 to 1.0% by weight of fine powder with a particle size of 0.2μ or less and a melting point of 90°C or higher is added to the pellet,
1000 to 300 with a high-speed stirrer such as a Henschel mixer.
In this method, a spherical molding material is obtained by stirring at 0 pm for 5 to 10 minutes.
以下詳細に説明する。This will be explained in detail below.
本発明に使用できる成形材料組成は、フェノール樹脂成
形材料、シアI) )レフタレート樹脂成形材料、アル
キド樹脂成形材料など一般の成形材料組成に適用でき、
特に充てん剤として31rLrfL以上の繊維、例えば
ビニロン繊維、ガラス繊維、アスベスト繊維などを50
%以上含む組成および使用樹脂の軟化点が80℃以下の
組成の材料を粒状化するときその効果を特に発揮する。The molding material composition that can be used in the present invention can be applied to general molding material compositions such as phenolic resin molding materials, shea I) phthalate resin molding materials, and alkyd resin molding materials.
In particular, as a filler, use fibers of 31rLrfL or higher, such as vinylon fibers, glass fibers, asbestos fibers, etc.
The effect is particularly exhibited when granulating materials having a composition containing % or more and a composition in which the softening point of the resin used is 80° C. or less.
成形材料組成物の混和は、従来のニーダ混和、ロール混
和、コニーダ混和などが適用できガラス繊維のように切
断しやすい繊維の場合は、湿式ニーダ混和が望ましい。Conventional kneader mixing, roll mixing, co-kneader mixing, etc. can be applied to the mixing of the molding material composition, and in the case of easily cuttable fibers such as glass fibers, wet kneader mixing is preferable.
前記方法で混和した成形材料組成物を温度70〜90℃
のロールで、厚さ2〜5mmのシート状にする、これを
ペレタイザなどで切断し、2〜51rLm角のペレット
とする。The molding material composition mixed in the above method is heated to a temperature of 70 to 90°C.
Roll it into a sheet with a thickness of 2 to 5 mm, and cut it with a pelletizer or the like to make pellets of 2 to 51 rLm square.
次に、このペレットに粒径0.2μ以下、融点90℃以
上の微粉末をペレットに対し0.2〜1.0%添加し、
ヘンシェルミキサーなどの高速攪拌機を使用して回転数
1000〜3000 pmで5〜10分間攪拌し球状の
成形材料を得る。Next, 0.2 to 1.0% of fine powder with a particle size of 0.2μ or less and a melting point of 90°C or more is added to the pellet,
A spherical molding material is obtained by stirring for 5 to 10 minutes at a rotation speed of 1,000 to 3,000 pm using a high-speed stirrer such as a Henschel mixer.
この時、高速攪拌機の温度は材料の軟化点以下であるこ
とが必要である。At this time, the temperature of the high speed stirrer must be below the softening point of the material.
本発明に使用する微粉末は粒径は0.2μ以下望ましく
は0.01μ以下が適当で、融点は90℃以上、望まし
くは90℃以上160℃以下が適当である。The fine powder used in the present invention has a particle size of 0.2 μm or less, preferably 0.01 μm or less, and a melting point of 90° C. or higher, preferably 90° C. or higher and 160° C. or lower.
粒径が大き過ぎると分散が不均一となり高速撹拌機回転
中ブロックしたり、成形後製品の外観、緒特性を低下す
る。If the particle size is too large, the dispersion becomes non-uniform, resulting in blockage during rotation of the high-speed stirrer, or deterioration of the appearance and properties of the molded product.
次に微粉末の融点は低過ぎると高速回転による摩擦熱の
ために材料表面に均一に分散する前に融けて、均一とな
らな(、成形品外観を低下させる。Next, if the melting point of the fine powder is too low, it will melt before it is evenly dispersed on the material surface due to the frictional heat caused by high-speed rotation, and the powder will not be uniform (this will deteriorate the appearance of the molded product).
また成形品の外観を重要視する場合、および添加量を多
くする場合は、融点90℃〜160℃が最適である。Furthermore, when the appearance of the molded product is important or when the amount added is large, a melting point of 90°C to 160°C is optimal.
このような微粉末には、ステアリン酸亜鉛、ステアリン
酸マグネシウム、ステアリン酸カルシウム、ステアリン
酸アルミニウム、微粉炭酸カルシウム、微粉シリカなど
がある。Such fine powders include zinc stearate, magnesium stearate, calcium stearate, aluminum stearate, finely divided calcium carbonate, finely divided silica, and the like.
次に微粉末の量はペレットに対し0.2〜1.0%が望
ましく、特に0.3〜0.5%が適当である。Next, the amount of fine powder is preferably 0.2 to 1.0%, particularly 0.3 to 0.5%, based on the pellet.
微粉末の量は少いと高速回転中ブロックしやす(、多過
ぎると外観その他諸特性を低下させる。If the amount of fine powder is small, it will easily block during high-speed rotation (too much will deteriorate the appearance and other properties).
なお、本方法によって得られた成形材料は射出成形のみ
でな(、移送成形、圧縮成形にも使用できる。The molding material obtained by this method can be used not only for injection molding, but also for transfer molding and compression molding.
以下本発明の実施例に基づいて具体的に説明する。The present invention will be specifically explained below based on examples.
実施例 1
軟化点80℃の低軟化点ポリエステル樹脂24部、ジア
リルフタレートモノマー4部、ジクミルパーオキサイド
0.6部、長さ1O−fIL7ILのガラス繊維14部
、炭酸カルシウム12部、水和アルミナ40部を80℃
の二−タ沖で20分間混和し、得られたアルキド成形材
料混和物をロールを使用して、温度60℃で厚さ5m1
1Lのシート状にし、このシートをペレタイザーで5m
m角のペレットにする3このペレットに対し0.3%の
ステアリン酸亜鉛を添加して水冷しであるヘンシェルミ
キサ内で回転数300Orpmで5分間攪拌して球状の
アルキド成形材料を得た。Example 1 24 parts of a low softening point polyester resin with a softening point of 80°C, 4 parts of diallyl phthalate monomer, 0.6 parts of dicumyl peroxide, 14 parts of glass fiber with a length of 1O-fIL7IL, 12 parts of calcium carbonate, hydrated alumina 40 parts at 80℃
The resulting alkyd molding material mixture was mixed for 20 minutes at a temperature of 60°C to a thickness of 5 m1 using a roll.
Make it into a 1L sheet and use a pelletizer to make it into a 5m sheet.
Forming m-square pellets 3. To the pellets, 0.3% zinc stearate was added and stirred in a water-cooled Henschel mixer at a rotational speed of 300 rpm for 5 minutes to obtain a spherical alkyd molding material.
本材料はホッパからシリンダ内への材料供給が安定し、
連続成形性に優れている。This material has a stable supply of material from the hopper into the cylinder.
Excellent continuous moldability.
射出成形条件を表1に示し、得られた特性を表2に示す
。The injection molding conditions are shown in Table 1, and the obtained properties are shown in Table 2.
なお、参考例として上記ロールで得られたシートをハン
マーミル型粉砕機を使用し、スクリーン8ψで粉砕する
と、低軟化点樹脂のため粉砕不可能であった。As a reference example, when the sheet obtained with the above roll was pulverized using a hammer mill type pulverizer with a screen of 8 ψ, it was impossible to pulverize it because of the low softening point resin.
実施例 2
ノボラック樹脂50部、ヘキサミン75部、ステアリン
酸亜鉛1.3部、消石灰2部、木粉18部、アスベスト
9.6部、長さ3T/L1nのビニロン10部、スピリ
ットブラック1部、フルフラール2部をブレンダーで均
一に混合し、前ロール90℃、後ロール80℃のロール
で7分間ロール混合し、直ちにペレタイザーで5mm角
のペレットにする。Example 2 50 parts of novolak resin, 75 parts of hexamine, 1.3 parts of zinc stearate, 2 parts of slaked lime, 18 parts of wood flour, 9.6 parts of asbestos, 10 parts of vinylon having a length of 3T/L1n, 1 part of spirit black, 2 parts of furfural are uniformly mixed in a blender, rolled for 7 minutes with a front roll at 90°C and a rear roll at 80°C, and immediately made into 5 mm square pellets using a pelletizer.
このペレットに対し0.3%のステアリン酸亜鉛を添加
し、ヘンシェルミキサーで回転数200 Orpm 5
分間攪拌し、ビニロン充てん剤の高衝撃強度を有する粒
状射出用フェノール成形材料を得た。0.3% zinc stearate was added to the pellets, and the mixture was mixed with a Henschel mixer at 200 rpm 5.
After stirring for a minute, a granular injection phenolic molding material with high impact strength of vinylon filler was obtained.
上記方法で得られた成形材料は、名機製作所RJ−75
Aで連続成形可能である。The molding material obtained by the above method is Meiki Seisakusho RJ-75
Continuous molding is possible at A.
本発明により、従来粒状化が困難であった長繊維含有熱
硬化性樹脂組成物、低軟化点熱硬化性樹脂酸物からも容
易に粒状の成形材料を得られるようになった。According to the present invention, it has become possible to easily obtain granular molding materials from long fiber-containing thermosetting resin compositions and low softening point thermosetting resin acids, which were conventionally difficult to granulate.
なお、本発明は上記熱硬化性樹脂組成物に限定されるも
のではなく、通常の熱硬化性樹脂組成物からも粒状成形
材料を得ることができるのはいうまでもない。Note that the present invention is not limited to the above-mentioned thermosetting resin composition, and it goes without saying that a granular molding material can also be obtained from an ordinary thermosetting resin composition.
Claims (1)
混練シート化した後ベレット状に切断し、これに融点9
0℃以上で粒径0.2μ以下の微粉末を添加し、高速攪
拌機で攪拌し造粒することを特徴とする熱硬化性樹脂成
形材料の製造方法。1 Add fillers and other additives to thermosetting resin,
After kneading into a sheet, cut it into pellets and give it a melting point of 9.
A method for producing a thermosetting resin molding material, which comprises adding fine powder having a particle size of 0.2 μm or less at a temperature of 0° C. or higher, and stirring and granulating the mixture with a high-speed stirrer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12802775A JPS5825571B2 (en) | 1975-10-23 | 1975-10-23 | Netsukou Kaseiji Yushisei Keizai Ryouno Seizouhouhou |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12802775A JPS5825571B2 (en) | 1975-10-23 | 1975-10-23 | Netsukou Kaseiji Yushisei Keizai Ryouno Seizouhouhou |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5251447A JPS5251447A (en) | 1977-04-25 |
JPS5825571B2 true JPS5825571B2 (en) | 1983-05-28 |
Family
ID=14974675
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12802775A Expired JPS5825571B2 (en) | 1975-10-23 | 1975-10-23 | Netsukou Kaseiji Yushisei Keizai Ryouno Seizouhouhou |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5825571B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102146379B1 (en) | 2019-03-04 | 2020-08-21 | 고려대학교 산학협력단 | Apparatus for management of cryopreserved cells and method thereof |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8621094D0 (en) * | 1986-09-01 | 1986-10-08 | Ici Plc | Loading of polymer additives |
-
1975
- 1975-10-23 JP JP12802775A patent/JPS5825571B2/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102146379B1 (en) | 2019-03-04 | 2020-08-21 | 고려대학교 산학협력단 | Apparatus for management of cryopreserved cells and method thereof |
Also Published As
Publication number | Publication date |
---|---|
JPS5251447A (en) | 1977-04-25 |
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