JPH0778156B2 - Acetal resin composition - Google Patents
Acetal resin compositionInfo
- Publication number
- JPH0778156B2 JPH0778156B2 JP61122125A JP12212586A JPH0778156B2 JP H0778156 B2 JPH0778156 B2 JP H0778156B2 JP 61122125 A JP61122125 A JP 61122125A JP 12212586 A JP12212586 A JP 12212586A JP H0778156 B2 JPH0778156 B2 JP H0778156B2
- Authority
- JP
- Japan
- Prior art keywords
- acetal resin
- molecular weight
- resin composition
- higher fatty
- fatty acid
- 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 - Lifetime
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- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、アセタール樹脂の本来有する機械的性質、熱
安定性及び成形品外観を実質的に全く損なわずして射出
成形の際の離型性を極めて高度に改善したアセタール樹
脂組成物に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention provides a mold release during injection molding without substantially impairing the mechanical properties, thermal stability and appearance of a molded article originally possessed by an acetal resin. The present invention relates to an acetal resin composition having extremely improved properties.
アセタール樹脂は、バランスのとれた機械的性質、優れ
た耐摩擦摩耗性、優れた耐熱性等の特性を有していると
共に、流動性にも極めて優れているため、射出成形によ
って複雑な構造の機械部品や精密機構部品とすることが
多く、斯かる複雑構造は、例えば、厚肉部と薄肉部、更
には超薄肉部が互いに入り組んだ上に、更に中空円筒状
突起物等が備わっている等の形状であり、しかも数gか
ら高々数10g程度の重量の小物部品である場合が多い。Acetal resin has well-balanced mechanical properties, excellent friction and wear resistance, excellent heat resistance, etc., and also has excellent fluidity. It is often a mechanical component or precision mechanical component, and such a complicated structure has, for example, a thick-walled portion, a thin-walled portion, and further, an ultra-thin-walled portion intertwined with each other, and a hollow cylindrical protrusion or the like. In many cases, it is a small part having a shape such as having a shape, and having a weight of several grams to at most several tens of grams.
このような複雑な形状の成形品の場合、成形品の突出し
離型は出来るだけスムーズでなければならず、製品を過
度に強い力で突出し離型した場合には、製品が破損され
たり成形ひずみを製品内部に保存して長期使用時に影響
が悪く露呈するという極めて好ましくない結果となるた
め、離型性の改善が切に望まれている。In the case of a molded product with such a complicated shape, the ejection of the molded product must be as smooth as possible, and if the product is ejected and released with an excessively strong force, the product will be damaged or the molding distortion will occur. Therefore, it is very desirable to improve the releasability, since the result is that the product is stored inside the product and the effect is bad and the product is exposed during long-term use.
離型性の改善提案は、これまでに幾つか為されており、
例えば、特公昭44−7544号には、低分子量炭化水素をア
セタール樹脂を添加することが、また特公昭45−31020
号には、高級脂肪酸アミドをアセタール樹脂に添加する
ことが各々提案されている。Several proposals for improvement of releasability have been made so far,
For example, in JP-B-44-7544, it is possible to add an acetal resin to a low molecular weight hydrocarbon, and JP-B-45-31020.
It is proposed that the higher fatty acid amide be added to the acetal resin.
しかしながら、これらの公知技術における離型効果は、
必ずしも市場の要請に十分応えるものではなく、更なる
離型性の改良が望まれていた。However, the releasing effect in these known techniques is
It does not always meet the market demand, and further improvement in releasability has been desired.
本発明者らは、これら従来技術の欠点に鑑み、鋭意研究
の結果、各々単独では効果の乏しい低分子量炭化水素と
高級脂肪酸アミドとを併用した場合、著しい相乗効果を
示すことを見出し、本発明に到達した。In view of these shortcomings of the prior art, the present inventors have found as a result of earnest research that when a low-molecular-weight hydrocarbon and a higher fatty acid amide, which are poor in effect alone, are used in combination, a remarkable synergistic effect is exhibited. Reached
即ち本発明は、アセタール樹脂に分子量200〜1800の低
分子量炭化水素と炭素数7〜24の高級脂肪酸アミドとを
添加してなるアセタール樹脂組成物である。That is, the present invention is an acetal resin composition obtained by adding a low molecular weight hydrocarbon having a molecular weight of 200 to 1800 and a higher fatty acid amide having a carbon number of 7 to 24 to an acetal resin.
本発明の組成物で用いられる分子量200〜1800の低分子
量炭化水素は、通常石油系パラフィンと呼ばれているも
のであり、一方炭素数7〜24の高級脂肪酸アミドは、炭
素数7〜24の高級脂肪酸と脂肪族アミンとの化合物であ
って、エチレンビスステアロアミド、ステアリン酸アミ
ド、ベヘン酸アミド及びオレイン酸アミドが特に好まし
いものである。The low molecular weight hydrocarbon having a molecular weight of 200 to 1800 used in the composition of the present invention is generally called petroleum paraffin, while the higher fatty acid amide having a carbon number of 7 to 24 has a carbon number of 7 to 24. Among the compounds of higher fatty acids and aliphatic amines, ethylene bis stearoamide, stearic acid amide, behenic acid amide and oleic acid amide are particularly preferable.
アセタール樹脂に対する低分子量炭化水素及び高級脂肪
酸アミドの添加量は、アセタール樹脂100重量部に対
し、各々が0.02〜1.00重量部であり、合計量として0.04
〜1.02重量部である範囲が適当である。これらの下限値
未満の量では効果が実用上不十分であり、一方上限度を
超える量ではアセタール樹脂の本来の性質の内の、特に
熱安定性及び成形外観(色調)の悪化をもたらす。The addition amount of the low molecular weight hydrocarbon and the higher fatty acid amide to the acetal resin is 0.02 to 1.00 parts by weight with respect to 100 parts by weight of the acetal resin, and the total amount is 0.04.
A range of up to 1.02 parts by weight is suitable. If the amount is less than these lower limits, the effect is practically insufficient, whereas if the amount exceeds the upper limit, the thermal stability and the molding appearance (color tone) are deteriorated among the original properties of the acetal resin.
本発明の組成物で用いられるアセタール樹脂とは、ホル
ムアルデヒド単量体又はその3量体(トリオキサン)若
しくは4量体(テトラオキサン)等の環状オリゴマーを
原料として製造された、実質的にオキシメチレン単位か
らなるオキシメチレンホモポリマー、及び、上記原料と
エチレンオキサイド、プロピレンオキサイド、エピクロ
ルヒドリン、1,3−ジオキソラン、1,3−ジオキセパン、
グリコールのホルマール、ジグリコールのホルマール等
の環状エーテルとから製造された、炭素数2〜8のオキ
シアルキレン単位を0.1〜20重量%含有するオキシメチ
レンコポリマーを包含する。The acetal resin used in the composition of the present invention refers to a formaldehyde monomer or a trimer (trioxane) or tetramer (tetraoxane) thereof, which is produced from a cyclic oligomer as a raw material. Oxymethylene homopolymer consisting of, and the above raw materials and ethylene oxide, propylene oxide, epichlorohydrin, 1,3-dioxolane, 1,3-dioxepane,
An oxymethylene copolymer containing 0.1 to 20% by weight of an oxyalkylene unit having 2 to 8 carbon atoms, which is produced from a cyclic ether such as glycol formal or diglycol formal.
本発明の組成物には、更に熱安定剤、酸化防止剤、紫外
線吸収剤、顔料、充填剤、ガラス繊維、炭素繊維その他
の公知の添加剤を配合することも出来る。The composition of the present invention may further contain heat stabilizers, antioxidants, ultraviolet absorbers, pigments, fillers, glass fibers, carbon fibers and other known additives.
本発明のアセタール樹脂組成物を製造する方法は各種採
用できるが、各成分を混合叉は溶融混練することは必須
である。Although various methods for producing the acetal resin composition of the present invention can be adopted, it is essential to mix or melt-knead each component.
溶融混練のために使用される装置としては、各種押出
機、ニーダー、バンバリー・ミキサー、ミキシングロー
ル等の一般的な混練機が用いられ、その際の混練方法と
しては、V字型ブレンダーの如き緩やかな混合装置叉は
ヘンシェルミキサーの如き高速流動混合装置によりドラ
イブレンドするか、叉は溶液、乳化液、懸濁液等の状態
で攪拌混合した後に乾燥して得た混合物を上記の混練機
に投入する方法、上記の混練機により均質な溶融状態の
アセタール樹脂組成物に低分子量炭化水素及び高級脂肪
酸アミドを添加する方法、ペレット状態のアセタール樹
脂組成物と低分子量炭化水素及び高級脂肪酸アミドとを
ドライブレンドした混合物を成形機に直接供給する方法
等がある。As an apparatus used for melt-kneading, a general kneading machine such as various extruders, kneaders, Banbury mixers, mixing rolls, etc. is used, and the kneading method at that time is a gentle kneading method such as a V-shaped blender. Mixing device or dry blending with a high-speed fluidized mixing device such as a Henschel mixer, or mixing with stirring in a state of solution, emulsion, suspension, etc., and then drying the resulting mixture is charged into the above kneader. Method, a method of adding a low molecular weight hydrocarbon and higher fatty acid amide to a homogeneous melted acetal resin composition by the above kneader, dry pelletized acetal resin composition and low molecular weight hydrocarbon and higher fatty acid amide There is a method of directly supplying the blended mixture to a molding machine.
溶融混練の温度は、用いるアセタール樹脂の種類、混合
混練装置の機能等の各種条件及び目的によって適当に選
定されるが、アセタール樹脂の融点以上分解温度以下及
び各種添加剤の分解温度以下の温度範囲であり、一般に
175〜230℃が適当である。The temperature of the melt-kneading is appropriately selected according to various conditions such as the type of acetal resin to be used, the function of the mixing and kneading device, and the purpose, but the temperature range of the melting point of the acetal resin or higher and the decomposition temperature or lower and the decomposition temperature of various additives or lower And in general
175-230 ° C is suitable.
本発明の組成物において、単独では希薄な効果しか示さ
ない低分子量炭化水素及び高級脂肪酸アミドとが優れた
効果をもたらす理由は明らかではないが、それぞれの単
独添加の場合に比べて、アセタール樹脂に対する相溶性
がより適度なものとなる結果、金型キャビティ面と樹脂
との境界面で容易に離型しうるある種の層を形成する為
でないかと推測される。In the composition of the present invention, it is not clear why low molecular weight hydrocarbons and higher fatty acid amides, which show only a dilute effect by themselves, bring about excellent effects. It is speculated that, as a result of the more appropriate compatibility, it is necessary to form a kind of layer that can be easily released at the interface between the mold cavity surface and the resin.
次に実施例及び比較例により本発明を更に詳細に説明す
る。Next, the present invention will be described in more detail with reference to Examples and Comparative Examples.
尚、以下の記載に於いて、極限粘度〔η〕は2重量%の
α−ピネンを添加したp−クロロフェノール中に於いて
60℃で測定した値を示し、添加量〔phr〕はアセタール
樹脂100重量部あたりの重量部を示す。In addition, in the following description, the intrinsic viscosity [η] is in p-chlorophenol to which 2% by weight of α-pinene is added.
The value measured at 60 ° C. is shown, and the addition amount [phr] is parts by weight per 100 parts by weight of the acetal resin.
又、第2表中の各試験は次の方法で行った。Each test in Table 2 was conducted by the following method.
離型力 成形品形状:高さ27mm、外径34mm、厚さ2mmの有低円筒
形 離型力:円筒底中心部に位置した突出しピンに接続した
センサーより感受 離型力測定センサー:(株)テクノ・プラス製 成形条件:射出成形機;(株)東芝製IS−90B 射出圧力;800kg/cm2 金型温度;60℃ 比率:実施例1の離型力に対する離型力の比率 初期色調 色差計:ハンター色差計((株)スガ試験機製) 離型剤添加前の成形品色調=L1、a1、b1 離型剤添加後の成形品色調=L1、a1、b1 算出式: 判断基準:◎;△E=0〜1 ○;△E=1超〜2 △;△E=2超〜3 ×;△E=3超〜4 滞留色調 色差計:ハンター色差計((株)スガ試験機製) 射出成形機:名機製作所製SJ−35A 滞留条件:材料温度;235℃ 滞留時間;60分間 滞留前の成形品色調=L3、a3、b3 滞留後の成形品色調=L4、a4、b4 算出式: 判断基準:◎;△E=0〜4 ○;△E=4超〜6 △;△E=6超〜8 ×;△E=8超〜10 熱安定性 使用機器:(株)島津製作所製DT−30 試験:222℃、空気中に於ける熱分解速度 引張衝撃強度 試験片成形条件:成形機;名機製作所製SJ−35A 材料温度;200℃ 射出圧力;500kg/cm2 金型温度;80℃ 実施例1〜9及び比較例1〜2 〔η〕=1.4dl/gの、エチレンオキシドから誘導される
共重合体を2.5重量%含有するオキシメチレンコポリマ
ーであるアセタール樹脂に、熱酸化安定剤としてのメラ
ミン0.2phr、立体障害性フェノール(チバ・ガイキー社
製イルガノックス1010)0.4phr及び水酸化マグネシウム
0.1phr並びに第1表に記載した種類及び量の低分子量炭
化水素及び高級脂肪酸アミドを添加したアセタール樹脂
組成物を、L/D=30、直径50mmのベント付二軸押出機を
用いて製造した。Releasing force Molded product shape: Height 27 mm, outer diameter 34 mm, thickness 2 mm Low cylinder type Releasing force: Sensitive from the sensor connected to the protruding pin located at the center of the cylindrical bottom Releasing force measuring sensor: (stock ) Techno plus manufactured by molding conditions: injection molding machine; Toshiba Ltd. IS-90B injection pressure: 800 kg / cm 2 mold temperature; 60 ° C. ratio: ratio initial color tone of the release force to release force of example 1 Color difference meter: Hunter color difference meter (manufactured by Suga Test Instruments Co., Ltd.) Color of molded product before release agent added = L 1 , a 1 , b 1 Color of molded product after release agent added = L 1 , a 1 , b 1 Calculation formula: Judgment Criteria: ◎; △ E = 0 to 1 ○; △ E = 1 over to 2 △; △ E = over 2 to 3 ×; △ E = over 3 to 4 Residence color tone color difference meter: Hunter color difference meter (Co., Ltd.) manufactured by Suga test Instruments Co.) injection molding machine: Meiki Ltd. SJ-35A residence conditions: material temperature; 235 ° C. the residence time; before dwell 60 minutes moldings color = L 3, a 3, b 3 residence after the molded product color = L 4 , a 4 , b 4 calculation formula: Judgment criteria: ◎; △ E = 0 to 4 ○; △ E = over 4 to 6 △; △ E = over 6 to 8 ×; △ E = over 8 to 10 Thermal stability Equipment used: Shimadzu Corporation DT-30 test: Pyrolysis rate in air at 222 ℃, Tensile impact strength Test piece molding conditions: Molding machine; SJ-35A made by Meiki Seisakusho Material temperature; 200 ℃ Injection pressure; 500kg / cm 2 Mold temperature; 80 ° C. Examples 1 to 9 and Comparative Examples 1 to 2 [η] = 1.4 dl / g, acetal resin which is an oxymethylene copolymer containing 2.5% by weight of a copolymer derived from ethylene oxide, and a thermal oxidation stabilizer. Melamine 0.2 phr, sterically hindered phenol (Irganox 1010 manufactured by Ciba-Gayky) 0.4 phr and magnesium hydroxide
An acetal resin composition containing 0.1 phr and the types and amounts of low molecular weight hydrocarbons and higher fatty acid amides listed in Table 1 was prepared using a vented twin screw extruder with L / D = 30 and a diameter of 50 mm. .
得られた試料について、離型力、成形品外観(色調)、
熱安定性及び引張衝撃強度を測定し、その結果を、実施
例1〜9として第2表に示した。For the obtained sample, the releasing force, the appearance (color tone) of the molded product,
The thermal stability and tensile impact strength were measured and the results are shown in Table 2 as Examples 1-9.
又、比較の為、低分子量炭化水素及び高級脂肪酸アミド
の何れか一方を添加しない場合の例及びその結果を、比
較例1〜2として第1表及び第2表に示した。For comparison, Tables 1 and 2 show Comparative Examples 1 and 2 in which one of the low molecular weight hydrocarbon and the higher fatty acid amide was not added and the results thereof.
実施例10 〔η〕=1.4dl/gの、エチレンオキシドから誘導される
共重合単位を2.5重量%含有するオキシメチレンコポリ
マーに、熱酸化安定剤としてのメラミン0.2phr、立体障
害性フェノール(チバ・ガイキー社製イルガノックス10
10)0.4phr及び水酸化マグネシウム0.1phrを添加してな
るペレット状の安定化アセタール樹脂組成物を、第1表
に記載した種類及び量の低分子量炭化水素及び高級脂肪
酸アミドと共に、ヘンシエルミキサー(三井三池(株)
製)に入れて高速混合した後、L/D=30、直径50mmのベ
ント付二軸押出機を用いて溶融混練し、アセタール樹脂
組成物を得た。Example 10 [η] = 1.4 dl / g in an oxymethylene copolymer containing 2.5% by weight of copolymerized units derived from ethylene oxide, 0.2 melamine as a thermal oxidation stabilizer, and a sterically hindered phenol (Ciba-Gayky) Company Irganox 10
10) A stabilized acetal resin composition in the form of pellets obtained by adding 0.4 phr and 0.1 phr of magnesium hydroxide, together with low molecular weight hydrocarbons and higher fatty acid amides of the types and amounts shown in Table 1, in a Hensiel mixer ( Mitsui Miike Co., Ltd.
(Made by Mfg. Co., Ltd.) and mixed at high speed, and then melt-kneaded using a twin-screw extruder with a vent having an L / D = 30 and a diameter of 50 mm to obtain an acetal resin composition.
得られた試料について、実施例1の場合と同様の試験を
実施し、その結果を、実施例10として第2表に示した。The same test as in Example 1 was performed on the obtained sample, and the result is shown in Table 2 as Example 10.
実施例11及び比較例3〜4 アセタール樹脂が、〔η〕=1.4dl/gの、1,3−ジオキセ
パンから誘導される共重合単位を3.5重量%含有するオ
キシメチレンコポリマーであること以外は、実施例1と
同様に実施し、その結果を実施例11として第2表に示し
た。Example 11 and Comparative Examples 3 to 4, except that the acetal resin is an oxymethylene copolymer containing 3.5 wt% of [η] = 1.4 dl / g of copolymerized units derived from 1,3-dioxepane. The same procedure as in Example 1 was carried out, and the result is shown in Table 2 as Example 11.
又、比較の為、低分子量炭化水素及び高級脂肪酸アミド
の何れか一方を添加しない場合の例及びその結果を、比
較例3〜4として第1表及び第2表に示した。For comparison, Tables 1 and 2 show Comparative Examples 3 to 4 in which no low molecular weight hydrocarbon or higher fatty acid amide was added and the results thereof.
実施例12及び比較例5〜6 アセタール樹脂が、〔η〕=1.3dl/gの、無水酢酸によ
り末端水酸基がアセチル化されたオキシメチレンホモポ
リマーであること以外は、実施例1と同様に実施し、そ
の結果を実施例12として第2表に示した。Example 12 and Comparative Examples 5-6 The same procedure as in Example 1 was carried out except that the acetal resin was an oxymethylene homopolymer in which the terminal hydroxyl group was acetylated with acetic anhydride, with [η] = 1.3 dl / g. The results are shown in Table 2 as Example 12.
又、比較の為、低分子量炭化水素及び高級脂肪酸アミド
の何れか一方を添加しない場合の例及びその結果を、比
較例5〜6として第1表及び第2表に示した。For comparison, Tables 1 and 2 show Comparative Examples 5 and 6 as examples and the results when neither low molecular weight hydrocarbons nor higher fatty acid amides were added.
Claims (2)
子量炭化水素と炭素数7〜24の高級脂肪酸アミドとを添
加してなるアセタール樹脂組成物1. An acetal resin composition obtained by adding a low molecular weight hydrocarbon having a molecular weight of 200 to 1800 and a higher fatty acid amide having a carbon number of 7 to 24 to an acetal resin.
量炭化水素及び高級脂肪酸アミドの個々の添加量が何れ
も0.02〜1.00重量部であり、合計の添加量が0.04〜1.02
重量部である特許請求の範囲第(1)項記載のアセター
ル樹脂組成物2. The low molecular weight hydrocarbon and the higher fatty acid amide are added individually in an amount of 0.02 to 1.00 parts by weight with respect to 100 parts by weight of the acetal resin, and the total amount added is 0.04 to 1.02.
The acetal resin composition according to claim (1), which is parts by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61122125A JPH0778156B2 (en) | 1986-05-29 | 1986-05-29 | Acetal resin composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61122125A JPH0778156B2 (en) | 1986-05-29 | 1986-05-29 | Acetal resin composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62280253A JPS62280253A (en) | 1987-12-05 |
| JPH0778156B2 true JPH0778156B2 (en) | 1995-08-23 |
Family
ID=14828236
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61122125A Expired - Lifetime JPH0778156B2 (en) | 1986-05-29 | 1986-05-29 | Acetal resin composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0778156B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2845452B2 (en) * | 1988-07-18 | 1999-01-13 | 東レ株式会社 | Method for producing polyoxymethylene |
| US5952410A (en) * | 1995-09-06 | 1999-09-14 | Asahi Kasei Kogyo Kabushiki Kaisha | Polyacetal resin composition exhibiting high retentivity of mechanical strengths |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS48100442A (en) * | 1972-03-31 | 1973-12-18 |
-
1986
- 1986-05-29 JP JP61122125A patent/JPH0778156B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62280253A (en) | 1987-12-05 |
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