JPH0318653B2 - - Google Patents
Info
- Publication number
- JPH0318653B2 JPH0318653B2 JP11497283A JP11497283A JPH0318653B2 JP H0318653 B2 JPH0318653 B2 JP H0318653B2 JP 11497283 A JP11497283 A JP 11497283A JP 11497283 A JP11497283 A JP 11497283A JP H0318653 B2 JPH0318653 B2 JP H0318653B2
- Authority
- JP
- Japan
- Prior art keywords
- phenolic resin
- molding material
- mixture
- pellet
- parts
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/16—Auxiliary treatment of granules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2061/00—Use of condensation polymers of aldehydes or ketones or derivatives thereof, as moulding material
- B29K2061/04—Phenoplasts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
- B29K2105/16—Fillers
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Reinforced Plastic Materials (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
【発明の詳細な説明】
本発明はフエノール樹脂成形材料およびその製
造方法に関し、更に詳しくは、シリンダー、ロー
ル、パイプおよびその他の異形品をはじめとする
成形品、特に鏡状表面(表面粗さ0.15μ以下で且
つ10cm角当たりに存在する径10μ以上のボイド数
が5個以下の高精度表面)が要求される精密成形
品に好適に用いられるフエノール樹脂成形材料お
よびその製造方法に関する。
フエノール樹脂成形材料は、熱可塑性樹脂成形
材料に比較して熱時の機械的強度が優れると共
に、他の熱硬化性樹脂成形材料に比較しても、機
械的強度、耐熱性、物理性能に優れ且つ比較的安
価であるため、シリンダー、ロール、パイプ等の
種々の成形品の製造に用いられている。
そして、かかるフエノール樹脂成形材料は、充
填剤として、木粉、パルプ、アスベスト、炭酸カ
ルシウム、タルク、マイカ等が用いられ、これら
の充填剤をフエノール樹脂に混合した混合物を、
ペレツト状に形成して成形材料として用いる。
しかしながら、かかるフエノール樹脂成形材料
の押出成形においては、ペレツト状成形材料を用
いているため、ペレツト間に空隙が形成され、こ
れが押出工程中においてペレツト間の融着不良の
原因となり、ペレツト間に空隙を残したまま押出
され、鏡状表面を有する成形品を製造することが
できないという問題がある。そのため、ペレツト
間の融着不良を解消する目的で成形材料の溶融粘
度を下げるなどの手段も講じられたが、今度は押
出成形が困難になるという問題がある。
本発明は、かかる事情に基づいて発明されたも
のであつて、前記従来の問題を解決した鏡状表面
を有する精密成形品に好適に用いられる押出成形
用フエノール樹脂成形材料およびその製造方法を
提供することを目的とするものである。
本発明の特徴とするところは、フエノール樹脂
に充填剤を混合してなるペレツト状混合物の表面
に、フエノール樹脂の被覆層を設けたフエノール
樹脂成形材料とした点にあり、その製造方法にお
いて、フエノール樹脂を溶解してなる溶液をペレ
ツト状混合物の表面に塗布した後、脱溶媒する点
にある。
以下、本発明を詳細に説明する。
本発明におけるペレツト状混合物は、フエノー
ル樹脂に充填剤を混練(ロール、ニーダ、バンバ
リミキサ等によつて行なわれる。)したシート状
混合物を、ヘンシルミキサ等でペレツト化して得
られる。
フエノール樹脂としては、フエノール、クレゾ
ール、キシレン等のフエノール類又は糖密、リグ
ニン、ナフタリン、石油系芳香族炭化水素による
変性フエノール類とホルマリン、パラホルムアル
デヒド等のアルデヒド類とを所定のモル比に配合
し、塩酸、硫酸、シユウ酸のような酸性触媒下で
反応させた後、脱水煮詰して、固形状にしたノボ
ラツク型フエノール樹脂初期縮合物、あるいは、
水酸化ナトリウム、アンモニア、アミン等のアル
カリ性触媒下で反応させた後、減圧脱水して固形
状にしたレゾール型フエノール樹脂初期縮合物が
用いられ、ノボラツク型フエノール樹脂初期縮合
物の場合には硬化剤としてヘキサメチレンテトラ
ミンが併用して用いられる。
ヘキサメチレンテトラミンの配合割合は、ノボ
ラツク型フエノール樹脂初期縮合物100重量部
(以下、部と記す)に対して、10〜25部が好まし
い。この範囲を下限において外れると硬化反応が
充分に行なえず強度等の特性に劣り、上限におい
て外れると成形時にアンモニアの発生が多くな
り、成形品表面にふくれが生じたり、成形品に金
属腐蝕が生じ易くなる。
充填剤としては、基材(木粉、パルプ、アスベ
ストなど)、充填剤(シリカ、タルク、ケイソウ
土など)、可塑剤(フルフラール、スチレンな
ど)、硬化促進剤、滑剤(ステアリン酸、ステア
リン酸亜鉛、ポリエチレンワツクス、カルバナワ
ツクス、リシノール酸、オキシステアリン酸、オ
イイン酸、ラウリン酸などの脂肪酸のアミド化合
物などで1μ以下の微粉末のものがよい)、着色剤
などが適宜用いられるが、通常、フエノール樹脂
100部に対して、基材30〜150部、充填剤2〜30
部、可塑剤0.5〜2部、滑剤1〜10部、着色剤適
量が用いられる。
又、フエノール樹脂の被覆層は、フエノール樹
脂を溶解する溶媒、例えば、メタノール、エタノ
ール等のアルコールにフエノール樹脂を溶解した
溶液、例えばそのフエノール樹脂濃度が0.2〜1.0
Kg/の溶液を前記ペレツト状混合物の表面にコ
ーテイングした後、脱溶媒して得られる。フエノ
ール樹脂溶液濃度が前記範囲を下限において外れ
ると、被覆層の厚みが薄くなつてペレツト間の融
着不良を解消する効果は小さく、上限において外
れると、被覆層の厚みが厚くなつてペレツトの溶
融粘度が低下して押出成形性が悪くなる。
又、脱溶媒の方法としては、常圧又は真空下で
行なわれるが、効率の点からは真空下で行うのが
好ましい。この時、フエノール樹脂の硬化反応を
開始させないためにも、温度は80℃以下で行なう
のが好ましい。
尚、本発明におけるフエノール樹脂成形材料を
用いて押出成形する場合には、フエノール樹脂被
覆層と押出機のシリンダ等との粘着を防止するた
めに、あらかじめペレツト状成形材料100部に対
し前記滑剤0.5〜5部をまぶして用いることがで
きる。
次に、本発明を実施例に基づいて比較例と併せ
て説明する。
第1表の配合によりフエノール樹脂に充填剤を
混合(ロール混練、混練温度100℃)してシート
状混合物を製した後、これをヘンシルミキサにか
けペレツト状混合物とした。このペレツト状混合
物を用い、第1表に示す如き条件にて、ペレツト
状混合物の表面にフエノール樹脂被覆層を形成せ
しめて、フエノール樹脂成形材料を製した。
次に、このフエノール樹脂成形材料を用いて押
出成形により内径25mmφ、外径30mmφ、長さ150
mmのパイプ成形品を得、この成形品について表面
特性等を調べた。
その結果、本発明によれば、押出成形性に優れ
且つ鏡状表面を有する精密成形品の製造が可能と
なつた。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a phenolic resin molding material and a method for producing the same, and more particularly to molded products such as cylinders, rolls, pipes and other irregularly shaped products, particularly molded products with mirror-like surfaces (surface roughness of 0.15 The present invention relates to a phenolic resin molding material suitable for use in precision molded products that require a high-precision surface with a diameter of 10 μm or less and 5 or less voids with a diameter of 10 μm or more existing per 10 cm square, and a method for producing the same. Phenol resin molding materials have superior mechanical strength when heated compared to thermoplastic resin molding materials, and also have superior mechanical strength, heat resistance, and physical performance compared to other thermosetting resin molding materials. Moreover, since it is relatively inexpensive, it is used for manufacturing various molded products such as cylinders, rolls, and pipes. Such phenolic resin molding materials use wood flour, pulp, asbestos, calcium carbonate, talc, mica, etc. as fillers, and a mixture of these fillers mixed with phenolic resin,
It is formed into pellets and used as a molding material. However, in extrusion molding of such phenolic resin molding materials, since pellet-shaped molding materials are used, voids are formed between the pellets, which causes poor fusion between the pellets during the extrusion process, resulting in voids between the pellets. There is a problem in that the molded product is extruded with a mirror-like surface remaining, making it impossible to produce a molded product with a mirror-like surface. Therefore, measures have been taken to reduce the melt viscosity of the molding material in order to solve the problem of poor fusion between the pellets, but this poses the problem of making extrusion molding difficult. The present invention was invented based on the above circumstances, and provides a phenolic resin molding material for extrusion molding that is suitably used for precision molded products having a mirror-like surface, which solves the conventional problems, and a method for producing the same. The purpose is to A feature of the present invention is that it is a phenolic resin molding material in which a coating layer of phenolic resin is provided on the surface of a pellet-like mixture formed by mixing a phenolic resin with a filler. After applying a solution prepared by dissolving the resin onto the surface of the pellet-like mixture, the solvent is removed. The present invention will be explained in detail below. The pellet-like mixture in the present invention is obtained by pelletizing a sheet-like mixture obtained by kneading a phenolic resin with a filler (this is done using a roll, kneader, Banbury mixer, etc.) using a Henshil mixer or the like. The phenolic resin is a mixture of phenols such as phenol, cresol, and xylene, or phenols modified with molasses, lignin, naphthalene, and petroleum aromatic hydrocarbons, and aldehydes such as formalin and paraformaldehyde in a predetermined molar ratio. , a novolak-type phenolic resin initial condensate that is reacted under an acidic catalyst such as hydrochloric acid, sulfuric acid, or oxalic acid, and then dehydrated and boiled down to form a solid, or
A resol-type phenolic resin initial condensate is used, which is made into a solid by reacting under an alkaline catalyst such as sodium hydroxide, ammonia, or amine, and then dehydrated under reduced pressure.In the case of a novolak-type phenolic resin initial condensate, a curing agent Hexamethylenetetramine is used in combination. The blending ratio of hexamethylenetetramine is preferably 10 to 25 parts per 100 parts by weight (hereinafter referred to as parts) of the novolak type phenolic resin initial condensate. If the lower limit of this range is outside this range, the curing reaction will not be sufficient and properties such as strength will be inferior, and if it is outside of the upper limit, ammonia will be generated more during molding, causing blistering on the surface of the molded product and metal corrosion on the molded product. It becomes easier. Fillers include base materials (wood flour, pulp, asbestos, etc.), fillers (silica, talc, diatomaceous earth, etc.), plasticizers (furfural, styrene, etc.), hardening accelerators, lubricants (stearic acid, zinc stearate, etc.) , polyethylene wax, carbana wax, amide compounds of fatty acids such as ricinoleic acid, oxystearic acid, oleic acid, and lauric acid (preferably fine powders of 1μ or less), coloring agents, etc. are used as appropriate, but usually phenol is used. resin
100 parts, base material 30-150 parts, filler 2-30 parts
part, 0.5 to 2 parts of plasticizer, 1 to 10 parts of lubricant, and an appropriate amount of colorant. In addition, the phenolic resin coating layer is made of a solvent that dissolves the phenolic resin, for example, a solution in which the phenolic resin is dissolved in an alcohol such as methanol or ethanol, for example, the phenolic resin concentration is 0.2 to 1.0.
It is obtained by coating the surface of the pellet-like mixture with a solution of Kg/kg and then removing the solvent. If the concentration of the phenolic resin solution deviates from the above range at the lower limit, the thickness of the coating layer becomes thinner and the effect of eliminating poor fusion between the pellets is small; when it deviates from the upper limit, the thickness of the coating layer increases and the melting of the pellets becomes difficult. The viscosity decreases and extrusion moldability deteriorates. Further, the method for removing the solvent may be carried out under normal pressure or vacuum, but from the viewpoint of efficiency it is preferably carried out under vacuum. At this time, the temperature is preferably 80° C. or lower in order to prevent the curing reaction of the phenol resin from starting. When extrusion molding is performed using the phenolic resin molding material of the present invention, 0.5 of the above-mentioned lubricant is added to 100 parts of the pellet-shaped molding material in advance in order to prevent adhesion between the phenolic resin coating layer and the cylinder of the extruder. It can be used by sprinkling ~5 parts. Next, the present invention will be explained based on Examples together with Comparative Examples. A filler was mixed with the phenolic resin according to the formulation shown in Table 1 (roll kneading, kneading temperature 100°C) to prepare a sheet-like mixture, which was then passed through a Henshil mixer to form a pellet-like mixture. Using this pelleted mixture, a phenolic resin coating layer was formed on the surface of the pelleted mixture under the conditions shown in Table 1 to produce a phenolic resin molding material. Next, using this phenolic resin molding material, extrusion molding was performed to create a mold with an inner diameter of 25 mmφ, an outer diameter of 30 mmφ, and a length of 150 mm.
A pipe molded product of mm in diameter was obtained, and the surface characteristics and other properties of this molded product were investigated. As a result, according to the present invention, it has become possible to manufacture a precision molded product with excellent extrusion moldability and a mirror-like surface. 【table】
Claims (1)
ツト状混合物の表面に、フエノール樹脂の被覆層
を設けてなることを特徴とするフエノール樹脂成
形材料。 2 フエノール樹脂に充填剤を混合してなるペレ
ツト状混合物の表面に、フエノール樹脂溶液を塗
布した後、脱溶媒することを特徴とするフエノー
ル樹脂成形材料の製造方法。[Scope of Claims] 1. A phenolic resin molding material, characterized in that a coating layer of phenolic resin is provided on the surface of a pellet-like mixture formed by mixing a phenolic resin with a filler. 2. A method for producing a phenolic resin molding material, which comprises applying a phenolic resin solution to the surface of a pellet-like mixture formed by mixing a filler with a phenolic resin, and then removing the solvent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11497283A JPS606413A (en) | 1983-06-24 | 1983-06-24 | Phenol resin molding material and preparation thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11497283A JPS606413A (en) | 1983-06-24 | 1983-06-24 | Phenol resin molding material and preparation thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS606413A JPS606413A (en) | 1985-01-14 |
| JPH0318653B2 true JPH0318653B2 (en) | 1991-03-13 |
Family
ID=14651181
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11497283A Granted JPS606413A (en) | 1983-06-24 | 1983-06-24 | Phenol resin molding material and preparation thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS606413A (en) |
-
1983
- 1983-06-24 JP JP11497283A patent/JPS606413A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS606413A (en) | 1985-01-14 |
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