JPH04266917A - Oxymethylene multicomponent copolymer - Google Patents

Oxymethylene multicomponent copolymer

Info

Publication number
JPH04266917A
JPH04266917A JP2867291A JP2867291A JPH04266917A JP H04266917 A JPH04266917 A JP H04266917A JP 2867291 A JP2867291 A JP 2867291A JP 2867291 A JP2867291 A JP 2867291A JP H04266917 A JPH04266917 A JP H04266917A
Authority
JP
Japan
Prior art keywords
oxymethylene
copolymer
compound
component
ether
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.)
Granted
Application number
JP2867291A
Other languages
Japanese (ja)
Other versions
JP3109104B2 (en
Inventor
Yoshiki Makabe
芳樹 真壁
Toshihiro Hatsu
発 敏博
Yoshiyuki Yamamoto
善行 山本
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP03028672A priority Critical patent/JP3109104B2/en
Publication of JPH04266917A publication Critical patent/JPH04266917A/en
Application granted granted Critical
Publication of JP3109104B2 publication Critical patent/JP3109104B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain the title copolymer having high cycle moldability during injection molding and excellent mechanical properties, comprising trioxan, a specific cyclic ether compound and a specific compound such as styrene oxide. CONSTITUTION:The objective copolymer which is an oxymethylene multicomponent copolymer obtained by copolymerizing (A) trioxan with (B) a cyclic ether compound selected from ethylene oxide, 1,3-dioxolan, 1,3-dioxepan, 1,3,5-trioxepan and 1,3,6-trioxocane and (C) a compound selected from glycidyl phenyl ether, styrene oxide and glycidyl naphthyl ether, has correlation between a melting point Tm and temperature dropping crystallization temperature Tc satisfying the formula 15<=Tm-Tc<25( deg.C) and <=30mum spherulite size. The copolymer is preferably obtained by subjecting the components A, B and C to bulk polymerization under stirring by a self-cleaning type stirrer without using a solvent at all, deactivating a catalyst with a hindered amine compound and decomposing and removing unstable polymer ends.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は射出成形時のハイサイク
ル性と機械物性に優れたオキシメチレン多元共重合体に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an oxymethylene multi-component copolymer which exhibits excellent high cycle performance and mechanical properties during injection molding.

【0002】更に詳しくは、射出成形時の金型内での固
化温度が高いためサイクル時間が短縮して成形でき、か
つ球晶サイズが小さいために成形歪が小さくなり機械物
性が優れたオキシメチレン多元共重合体に関するもので
ある。
More specifically, oxymethylene has a high solidification temperature in the mold during injection molding, so it can be molded in a short cycle time, and its small spherulite size reduces molding distortion, resulting in excellent mechanical properties. It relates to multi-component copolymers.

【0003】0003

【従来の技術】ポリオキシメチレン樹脂は機械的強度と
耐衝撃性のバランスのとれたエンジニアリングプラスチ
ックとして知られ、自動車部品、電子機器用部品として
広範な分野において使用されている。
BACKGROUND OF THE INVENTION Polyoxymethylene resins are known as engineering plastics with a good balance of mechanical strength and impact resistance, and are used in a wide range of fields as parts for automobiles and electronic devices.

【0004】ポリオキシメチレン樹脂の加工は大部分射
出成形でなされている。この射出成形分野において、成
形サイクルの短縮化、いわゆるハイサイクル化による生
産性向上が強く要望されている。
Polyoxymethylene resins are mostly processed by injection molding. In the field of injection molding, there is a strong demand for improved productivity by shortening the molding cycle, so-called high cycle.

【0005】結晶性高分子であるポリオキシメチレン樹
脂のハイサイクル化には、核発生化剤を添加して結晶化
速度を速くし、金型内での固化速度を速める方法が提案
されている。例えば、特開昭59−129247号公報
や特公昭55−19942号公報では、分岐構造を有す
るポリオキシメチレン樹脂を核発生化剤として用いる方
法が記載されている。また、特公昭48−8254号公
報にはタルクに代表される無機化合物を核発生化剤とし
て添加することが記載されている。
[0005] To increase the cycle speed of polyoxymethylene resin, which is a crystalline polymer, a method has been proposed in which a nucleating agent is added to increase the crystallization rate and solidification rate in the mold. . For example, JP-A-59-129247 and JP-B-55-19942 describe a method using a polyoxymethylene resin having a branched structure as a nucleating agent. Furthermore, Japanese Patent Publication No. 48-8254 describes the addition of an inorganic compound typified by talc as a nucleating agent.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記特
開昭59−129247号公報、特公昭55−1994
2号公報、特公昭48−8254号公報に記載された樹
脂組成物は結晶化速度の向上が不十分であり、満足され
るハイサイクル性が望めないばかりか、更に得られた成
形品の結晶構造の微細化、均質化による機械的強度の向
上も不十分であり、電気・電子機器用品、自動車部品等
の用途に要求されるさらに高い機械的強度を満足するも
のではない。
[Problems to be Solved by the Invention] However, the above-mentioned Japanese Patent Application Laid-Open No. 129247/1982 and Japanese Patent Publication No. 55-1994
The resin compositions described in Publication No. 2 and Japanese Patent Publication No. 48-8254 do not improve the crystallization rate sufficiently, and not only cannot a satisfactory high cycle performance be expected, but also the crystallization of the obtained molded product is Improvement in mechanical strength by making the structure finer and more homogeneous is also insufficient, and does not satisfy the higher mechanical strength required for applications such as electrical and electronic equipment products and automobile parts.

【0007】[0007]

【課題を解決するための手段】本発明者らは、核発生化
剤を添加しないでハイサイクル性と機械物性に優れたポ
リオキシメチレン樹脂を得るべく鋭意検討した結果、本
発明に到達した。
[Means for Solving the Problems] The present inventors have conducted intensive studies to obtain a polyoxymethylene resin having excellent high cycle properties and mechanical properties without adding a nucleating agent, and as a result, they have arrived at the present invention.

【0008】即ち、本発明は(a)トリオキサンと(b
)エチレンオキシド、1,3−ジオキソラン、1,3−
ジオキセパン、1,3,5−トリオキセパン、1,3,
6−トリオキソカンから選ばれた少なくとも1種の環状
エーテル化合物及び(c)グリシジルフェニルエーテル
、スチレンオキシド、グリシジルナフチルエーテルから
選ばれた少なくとも1種の化合物を共重合して得られる
オキシメチレン多元共重合体であって、該オキシメチレ
ン多元共重合体の融点(Tm)と降温結晶化温度(Tc
)の関係が 15≦Tm−Tc<25    (℃)であり、かつ球
晶サイズが30μm以下の大きさであることを特徴とす
るオキシメチレン多元共重合体を提供するものである。
That is, the present invention provides (a) trioxane and (b)
) ethylene oxide, 1,3-dioxolane, 1,3-
Dioxepane, 1,3,5-trioxepane, 1,3,
An oxymethylene multicomponent copolymer obtained by copolymerizing at least one cyclic ether compound selected from 6-trioxocane and (c) at least one compound selected from glycidyl phenyl ether, styrene oxide, and glycidyl naphthyl ether. The melting point (Tm) and cooling crystallization temperature (Tc) of the oxymethylene multi-component copolymer are
The present invention provides an oxymethylene multi-component copolymer, which has the following relationship: 15≦Tm-Tc<25 (°C), and has a spherulite size of 30 μm or less.

【0009】本発明のオキシメチレン多元共重合体の製
造方法は特に限定されない。例えば(a)成分のトリオ
キサンと(b)成分のエチレンオキシド、1,3−ジオ
キソラン、1,3−ジオキセパン、1,3,5−トリオ
キセパン、1,3,6−トリオキソカンから選ばれた少
なくとも1種の環状エーテル化合物及び(c)成分のグ
リシジルフェニルエーテル、スチレンオキシド、グリシ
ジルナフチルエーテルから選ばれた少なくとも1種の化
合物をシクロヘキサンのような有機溶媒中に溶解、ある
いは懸濁した後、ルイス酸触媒を添加して重合し、不安
定末端を分解除去して製造することができる。好ましく
は溶媒を全く使用せずにセルフクリーニング型撹拌機を
使用して塊状重合し、ヒンダードアミン化合物で触媒失
活させた後、不安定末端を分解除去して製造する方法が
挙げられる。ルイス酸触媒としては、三フッ化ホウ素、
三フッ化ホウ素水和物および酸素または硫黄原子を有す
る有機化合物と三フッ化ホウ素との配位化合物が好まし
く使用される。ルイス酸触媒の添加量は、トリオキサン
100重量部に対して0.001〜0.1重量部の範囲
が好ましく、特に好ましくは0.005〜0.05重量
部の範囲である。また、塊状重合反応温度は60〜12
0℃の範囲が好ましく、特に60〜90℃の範囲が好ま
しい。触媒を失活させるヒンダードアミン化合物とは、
ビス(1,2,2,6,6−ペンタメチル−4−ピペリ
ジニル)セバケート、ビス(2,2,6,6−テトラメ
チル−4−ピペリジル)セバケート、コハク酸ジメチル
−1−(2−ヒドロキシエチル−2,2,6,6テトラ
メチルピペリジン重縮合物、1−[2−[3−(3,5
−ジ−t−ブチル−4−ヒドロキシフェニル)プロピオ
ニルオキシ]エチル]−4−[3−(3.5−ジ−t−
ブチル−4−ヒドロキシフェニル)プロピオニルオキシ
]−2,2,6,6−テトラメチルピペリジンなどのよ
うな分子中にヒンダードアミン骨格を有する化合物を意
味し、その添加量は、触媒のホウ素原子1個に対してヒ
ンダードアミン化合物中の窒素原子0.1〜20個に相
当する量を添加するのが好ましい。
The method for producing the oxymethylene multi-component copolymer of the present invention is not particularly limited. For example, at least one member selected from trioxane as the component (a) and ethylene oxide, 1,3-dioxolane, 1,3-dioxepane, 1,3,5-trioxepane, and 1,3,6-trioxocane as the component (b). A cyclic ether compound and at least one compound selected from glycidyl phenyl ether, styrene oxide, and glycidyl naphthyl ether as component (c) are dissolved or suspended in an organic solvent such as cyclohexane, and then a Lewis acid catalyst is added. It can be produced by polymerizing and decomposing and removing unstable ends. Preferably, there is a method of producing by bulk polymerizing using a self-cleaning stirrer without using any solvent, deactivating the catalyst with a hindered amine compound, and then decomposing and removing unstable terminals. As a Lewis acid catalyst, boron trifluoride,
Boron trifluoride hydrate and coordination compounds of boron trifluoride and organic compounds having oxygen or sulfur atoms are preferably used. The amount of Lewis acid catalyst added is preferably in the range of 0.001 to 0.1 part by weight, particularly preferably in the range of 0.005 to 0.05 part by weight, per 100 parts by weight of trioxane. Moreover, the bulk polymerization reaction temperature is 60 to 12
A temperature range of 0°C is preferred, and a range of 60 to 90°C is particularly preferred. What is a hindered amine compound that deactivates a catalyst?
Bis(1,2,2,6,6-pentamethyl-4-piperidinyl) sebacate, bis(2,2,6,6-tetramethyl-4-piperidyl) sebacate, dimethyl-1-(2-hydroxyethyl succinate) -2,2,6,6 tetramethylpiperidine polycondensate, 1-[2-[3-(3,5
-di-t-butyl-4-hydroxyphenyl)propionyloxy]ethyl]-4-[3-(3.5-di-t-
It refers to a compound having a hindered amine skeleton in the molecule, such as butyl-4-hydroxyphenyl)propionyloxy]-2,2,6,6-tetramethylpiperidine, and the amount added is per boron atom of the catalyst. It is preferable to add the amount corresponding to 0.1 to 20 nitrogen atoms in the hindered amine compound.

【0010】本発明のオキシメチレン多元共重合体にお
ける(b)成分のエチレンオキシド、1,3−ジオキソ
ラン、1,3−ジオキセパン、1,3,5−トリオキセ
パン、1,3,6−トリオキソカンから選ばれた少なく
とも1種の環状エーテル化合物の共重合量は十分に高い
機械的強度を得るために重要であり、これらの化合物に
由来するオキシアルキレン単位が、(b)成分のトリオ
キサン等から由来するオキシメチレン単位に対し、0.
01〜2.0モル%の範囲にあることが好ましい。0.
01モル%未満では熱安定性が低下し、2.0モル%を
越えると十分に優れた機械的強度を有するポリマを得る
ことが困難であるため好ましくない。
[0010] Component (b) in the oxymethylene multi-component copolymer of the present invention is selected from ethylene oxide, 1,3-dioxolane, 1,3-dioxepane, 1,3,5-trioxepane, and 1,3,6-trioxocane. The copolymerization amount of at least one cyclic ether compound is important in order to obtain sufficiently high mechanical strength. For the unit, 0.
It is preferably in the range of 0.01 to 2.0 mol%. 0.
If it is less than 0.01 mol%, the thermal stability will decrease, and if it exceeds 2.0 mol%, it will be difficult to obtain a polymer with sufficiently excellent mechanical strength, which is not preferred.

【0011】本発明のオキシメチレン多元共重合体にお
ける(c)成分のグリシジルフェニルエーテル、スチレ
ンオキシド、グリシジルナフチルエーテルから選ばれた
少なくとも1種の化合物の共重合量は、(a)成分のト
リオキサン等に由来するオキシメチレン単位に対し0.
001〜2.0モル%の範囲にあることが好ましく、特
に好ましくは0.01〜1.0モル%の範囲である。 0.001モル%未満ではハイサイクル性の改良効果が
小さく、2.0モル%を越えると機械的強度が低下する
ため好ましくない。
[0011] In the oxymethylene multi-component copolymer of the present invention, the copolymerized amount of at least one compound selected from glycidyl phenyl ether, styrene oxide, glycidyl naphthyl ether as component (c) is greater than the amount of trioxane, etc. as component (a). 0.0 for the oxymethylene unit derived from
It is preferably in the range of 0.001 to 2.0 mol%, particularly preferably in the range of 0.01 to 1.0 mol%. If it is less than 0.001 mol%, the effect of improving high cycle performance is small, and if it exceeds 2.0 mol%, mechanical strength will decrease, which is not preferable.

【0012】本発明のオキシメチレン多元共重合体の重
合度は、80℃の熱風オーブン中で3時間乾燥したペレ
ットを用い、ASTM  D1238に従って、温度1
90℃、荷重2160gで測定したMI値で、1〜60
g/10分の範囲にあることが好ましい。数平均分子量
に換算するとおよそ8,000〜100,000の範囲
にあることが好ましい。MI値が1g/10分より小さ
いと射出成形時の流動性が低下し、薄肉成形品が成形で
きないため好ましくない。また、60g/10分以上に
なると重合度が低いため、機械的強度が問題となるため
好ましくない。
The degree of polymerization of the oxymethylene multi-component copolymer of the present invention is determined according to ASTM D1238 using pellets dried in a hot air oven at 80°C for 3 hours.
MI value measured at 90℃ and a load of 2160g, 1 to 60
Preferably, it is in the range of g/10 minutes. The number average molecular weight is preferably in the range of approximately 8,000 to 100,000. If the MI value is less than 1 g/10 min, the fluidity during injection molding will decrease, making it impossible to mold a thin-walled molded product, which is not preferable. Moreover, if it exceeds 60 g/10 minutes, the degree of polymerization will be low and mechanical strength will become a problem, which is not preferable.

【0013】本発明のオキシメチレン多元共重合体が、
優れたハイサイクル成形性と機械物性を有するためには
、オキシメチレン多元共重合体の融点(Tm)と降温結
晶化温度(Tc)の関係が 15≦Tm−Tc<25    (℃)であり、かつ球
晶サイズが30μm以下の大きさであることが必要であ
る。Tmが低いためにTm−Tcが15℃未満の場合は
、十分に高い機械的強度を得ることが難しく、逆にTm
が高いためにTm−Tcが25℃以上の場合は、オキシ
メチレン共重合体が本来から持ち得る熱安定性が損なわ
れてしまうため好ましくない。また、Tcが高いために
Tm−Tcが15℃未満の場合は、靭性が大きく低下し
てしまい、逆にTcが低いためにTm−Tcが25℃以
上の場合は、射出成形後の残留歪が大きく、機械的強度
を低下させるため好ましくない。即ち、十分な高い機械
的強度を得るには(b)成分の共重合量はある程度以下
である必要があり、そのためTmが高くなるが、一方、
優れたハイサイクル性と高い機械的強度を得るために(
c)成分を共重合するとTcが高くなる。更に、球晶サ
イズが30μm以上になると射出成形後の残留成形歪が
大きく、機械物性を低下させるため好ましくない。
The oxymethylene multi-component copolymer of the present invention has
In order to have excellent high-cycle moldability and mechanical properties, the relationship between the melting point (Tm) and cooling crystallization temperature (Tc) of the oxymethylene multi-component copolymer is 15≦Tm-Tc<25 (°C), In addition, it is necessary that the spherulite size be 30 μm or less. If Tm-Tc is less than 15°C due to low Tm, it is difficult to obtain sufficiently high mechanical strength;
If Tm-Tc is 25° C. or higher due to high Tm-Tc, the inherent thermal stability of the oxymethylene copolymer will be impaired, which is not preferable. Furthermore, if Tm-Tc is less than 15°C due to high Tc, the toughness will be greatly reduced, and conversely, if Tm-Tc is 25°C or more due to low Tc, residual strain after injection molding will occur. is undesirable because it is large and reduces mechanical strength. That is, in order to obtain a sufficiently high mechanical strength, the amount of copolymerization of component (b) must be below a certain level, which increases Tm, but on the other hand,
In order to obtain excellent high cycle performance and high mechanical strength (
When component c) is copolymerized, Tc increases. Furthermore, if the spherulite size is 30 μm or more, residual molding distortion after injection molding is large and mechanical properties are deteriorated, which is not preferable.

【0014】本発明でのTmとTcの測定は、差動走査
熱量計(DSC)を使用して窒素雰囲気下、室温から1
0℃/分の速度で220℃まで昇温し、5分間220℃
で保持した後、10℃/分の速度で降温し、降温結晶化
温度(Tc)を測定した後、100℃まで冷却後再び1
0℃/分の速度で昇温して、融点(Tm)を測定する方
法を採用した。本発明のオキシメチレン多元共重合体の
Tmは155〜180℃の範囲にあることが好ましく、
特に好ましくは160〜175℃の範囲である。本発明
のオキシメチレン多元共重合体のTcは140〜155
℃の範囲にあることが好ましく、特に好ましくは145
〜152℃の範囲である。
[0014] In the present invention, Tm and Tc are measured using a differential scanning calorimeter (DSC) under a nitrogen atmosphere at room temperature.
Raise the temperature to 220°C at a rate of 0°C/min and leave at 220°C for 5 minutes.
After holding the temperature at
A method was adopted in which the temperature was raised at a rate of 0° C./min and the melting point (Tm) was measured. The Tm of the oxymethylene multi-component copolymer of the present invention is preferably in the range of 155 to 180°C,
Particularly preferably, the temperature is in the range of 160 to 175°C. Tc of the oxymethylene multi-component copolymer of the present invention is 140 to 155
It is preferably in the range of 145 °C, particularly preferably 145 °C.
-152°C.

【0015】また、球晶サイズは、オキシメチレン多元
共重合体約2mgをカバーガラスに挟み、ホットステー
ジ上で加熱して、230℃で5分間溶融させた後、偏光
顕微鏡で観察しながら10℃/分の速度で130℃まで
降温し、生成した結晶を写真撮影して球晶サイズを求め
る方法を採用した。
[0015] The spherulite size was determined by sandwiching about 2 mg of the oxymethylene multi-component copolymer between cover glasses, heating it on a hot stage, melting it at 230°C for 5 minutes, and then melting it at 10°C while observing it with a polarizing microscope. A method was adopted in which the temperature was lowered to 130°C at a rate of 1/min, and the spherulite size was determined by photographing the formed crystals.

【0016】また、本発明のオキシメチレン多元共重合
体には、本発明の目的を損なわない範囲で、公知のヒン
ダードフェノール系、ホスファイト系、チオエーテル系
、アミン系などの酸化防止剤、ベンゾフェノン系、ヒン
ダードアミン系などの耐候剤、メラミン、ジシアンジア
ミド、ポリアミド、ポリビニルアルコール共重合体など
のホルムアルデヒド捕捉剤、含フッ素系ポリマ、シリコ
ーンオイル、ポリエチレンワックスなどの減摩剤、染料
や顔料などの着色剤、酸化チタン、カーボンブラックな
どの紫外線遮蔽剤、ガラス繊維やカーボンファイバーチ
タン酸カリファイバーなどの強化剤、シリカ、クレー、
炭酸カルシウム、硫酸カルシウム、ガラスビーズなどの
充填剤、タルクなどの核剤、難燃剤、可塑剤、接着助剤
、粘着剤などを任意に含有せしめることができる。 更に、本発明のオキシメチレン多元共重合体の機械的強
度を向上する目的で他の熱可塑性ポリマや熱可塑性エラ
ストマを含有させることもできる。
In addition, the oxymethylene multi-component copolymer of the present invention may contain known antioxidants such as hindered phenol, phosphite, thioether, and amine antioxidants, and benzophenone, within a range that does not impair the purpose of the present invention. Weathering agents such as melamine, hindered amine, formaldehyde scavengers such as melamine, dicyandiamide, polyamide, and polyvinyl alcohol copolymers, antifriction agents such as fluorine-containing polymers, silicone oil, and polyethylene wax, coloring agents such as dyes and pigments, UV shielding agents such as titanium oxide and carbon black, reinforcing agents such as glass fiber and carbon fiber titanate potassium fiber, silica, clay,
Fillers such as calcium carbonate, calcium sulfate, and glass beads, nucleating agents such as talc, flame retardants, plasticizers, adhesion aids, adhesives, and the like can be optionally contained. Furthermore, for the purpose of improving the mechanical strength of the oxymethylene multi-component copolymer of the present invention, other thermoplastic polymers or thermoplastic elastomers may be contained.

【0017】[0017]

【実施例】以下に実施例により本発明の効果を説明する
[Example] The effects of the present invention will be explained below with reference to Examples.

【0018】なお、実施例中の%および部はすべて重量
基準である。また、成形サイクルや機械物性などは次の
ように測定した。
Note that all percentages and parts in the examples are based on weight. In addition, the molding cycle, mechanical properties, etc. were measured as follows.

【0019】・成形サイクル:5オンスの射出能力を有
する射出成形機を用いて、シリンダ温度190℃、金型
温度60℃、射出時間5秒に設定し、冷却時間を変更し
て80×80×3mmtの角板を成形し、4本の突き出
しピンによる変形が、平板上に成形品の3つの頂点を置
いた場合、残りの1つの頂点の平板からのずれが1mm
以下となる冷却時間を測定した。
- Molding cycle: Using an injection molding machine with an injection capacity of 5 ounces, the cylinder temperature was set to 190°C, the mold temperature was 60°C, and the injection time was 5 seconds.The cooling time was changed to 80×80× When a 3mmt square plate is molded and the three vertices of the molded product are placed on the flat plate due to deformation using four ejector pins, the deviation of the remaining one vertex from the flat plate is 1mm.
The following cooling times were measured.

【0020】・機械物性:5オンスの射出能力を有する
射出成形機を用いて、シリンダ温度190℃、金型温度
65℃、成形サイクル50秒に設定して、ASTM1号
ダンベル試験片を射出成形した。得られたASTM1号
ダンベル試験片を用い、ASTM  D638法に準じ
て引張強度を、ASTM  D790法に準じて曲げ弾
性率を測定した。
- Mechanical properties: ASTM No. 1 dumbbell test piece was injection molded using an injection molding machine with a 5 oz injection capacity, setting the cylinder temperature to 190°C, the mold temperature to 65°C, and the molding cycle to 50 seconds. . Using the obtained ASTM No. 1 dumbbell test piece, tensile strength was measured according to ASTM D638 method, and flexural modulus was measured according to ASTM D790 method.

【0021】実施例1〜5、比較例1〜5100mmφ
、L/D=10の2軸の連続型混合機(栗本鉄工所製“
KRCニーダ”S−4型)にトリオキサン、(b)成分
の化合物、(c)成分の化合物、およびトリオキサンに
対して100ppmの三フッ化ホウ素ジエチルエーテラ
ート(2.5%ベンゼン溶液)、重合度調節剤のメチラ
ールをそれぞれ供給し、連続重合を行なった。重合温度
は外部ジャケットに温水を通すことにより、約60℃に
コントロールし、回転数は60rpmに設定した。(c
)成分の化合物と分子量調節剤としてのメチラールは、
トリオキサン中に溶解した。又、(b)成分の化合物と
触媒溶液は、ニーダーへ供給する直前に予備混合される
ように予備混合ゾーンを設けた。重合体は白色微粉末と
して得られた。
Examples 1 to 5, Comparative Examples 1 to 5100mmφ
, 2-shaft continuous mixer with L/D=10 (manufactured by Kurimoto Iron Works)
Trioxane, the compound of component (b), the compound of component (c), and 100 ppm boron trifluoride diethyl etherate (2.5% benzene solution) with respect to trioxane were added to KRC kneader "S-4 type), and the degree of polymerization was Continuous polymerization was carried out by supplying each of the regulators, methylal. The polymerization temperature was controlled at approximately 60°C by passing hot water through the outer jacket, and the rotation speed was set at 60 rpm. (c
) component compound and methylal as a molecular weight regulator,
Dissolved in trioxane. Further, a premixing zone was provided so that the compound of component (b) and the catalyst solution were premixed immediately before being supplied to the kneader. The polymer was obtained as a white fine powder.

【0022】この様にして得られた微粉末10kgに対
して、27gのビス(1,2,2,6,6−ペンタメチ
ル−4−ピペリジニル)セバケートを200mlのベン
ゼンに溶解した溶液を添加して触媒失活を行った後、更
にステアリン酸カルシウム10g、1,6−ヘキサンジ
オール−ビス−〔3−(3,5−ジ−t−ブチル−4−
ヒドロキシフェニル)プロピオネート〕[チバ・ガイギ
−(Ciba−Geigy)社製“イルガノックス(I
rganox)”245]50gを添加してヘンシェル
ミキサー中で10分間撹拌した。得られた混合物を35
mmφ、L/D=30のベント付2軸押出機を使用して
、シリンダー温度230℃、ベントの真空度5Torr
の条件で溶融安定化を行った後、水中に吐出しカッティ
ングを行ってペレット状のオキシメチレン多元共重合体
を得た。得られたオキシメチレン多元共重合体の組成の
確認は60MHz  1H  NMR(重ヘキサフルオ
ロイソプロパノール溶媒中)で行った。例えば、(c)
成分の化合物としてグリシジルフェニルエーテルを用い
た場合、δ4.3−5.2(ppm)のメチレン基のシ
グナルの他にδ6.9−7.6(ppm)にフェニル基
特有のマルチプレットのシグナルが検出されることによ
り、グリシジルフェニルエーテル共重合体であることを
確認した。また。積分値により仕込量からほぼ定量的に
共重合されていることを確認した。このようにして得ら
れた各種オキシメチレン多元共重合体の共重合組成と物
性を表1に示す。
A solution of 27 g of bis(1,2,2,6,6-pentamethyl-4-piperidinyl) sebacate dissolved in 200 ml of benzene was added to 10 kg of the fine powder thus obtained. After deactivating the catalyst, 10 g of calcium stearate, 1,6-hexanediol-bis-[3-(3,5-di-t-butyl-4-
Hydroxyphenyl) propionate] [Irganox (I) manufactured by Ciba-Geigy
rganox)” 245] was added and stirred for 10 minutes in a Henschel mixer.
Using a vented twin-screw extruder with mmφ and L/D=30, the cylinder temperature was 230°C and the vent vacuum degree was 5 Torr.
After melt stabilization under these conditions, the mixture was discharged into water and cut to obtain a pellet-like oxymethylene multi-component copolymer. The composition of the obtained oxymethylene multi-component copolymer was confirmed by 60 MHz 1H NMR (in heavy hexafluoroisopropanol solvent). For example, (c)
When glycidylphenyl ether is used as a component compound, in addition to the methylene group signal at δ4.3-5.2 (ppm), there is a multiplet signal unique to phenyl groups at δ6.9-7.6 (ppm). By the detection, it was confirmed that it was a glycidyl phenyl ether copolymer. Also. It was confirmed by the integral value that the copolymerization was almost quantitative based on the amount charged. Table 1 shows the copolymer composition and physical properties of the various oxymethylene multi-component copolymers thus obtained.

【0023】[0023]

【表1】[Table 1]

【0024】表1の結果から本発明の多元共重合体が射
出成形性と機械物性に優れていることが明らかである。
From the results shown in Table 1, it is clear that the multi-component copolymer of the present invention has excellent injection moldability and mechanical properties.

【0025】[0025]

【発明の効果】本発明のオキシメチレン多元共重合体は
球晶サイズが小さく、成形歪の小さい、高い機械物性を
有するポリオキシメチレン樹脂成形品を提供する。
Effects of the Invention The oxymethylene multi-component copolymer of the present invention provides a polyoxymethylene resin molded article having a small spherulite size, low molding distortion, and high mechanical properties.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  (a)トリオキサンと(b)エチレン
オキシド、1,3−ジオキソラン、1,3−ジオキセパ
ン、1,3,5−トリオキセパン、1,3,6−トリオ
キソカンから選ばれた少なくとも1種の環状エーテル化
合物及び(c)グリシジルフェニルエーテル、スチレン
オキシド、グリシジルナフチルエーテルから選ばれた少
なくとも1種の化合物を共重合して得られるオキシメチ
レン多元共重合体であって、該オキシメチレン多元共重
合体の融点(Tm)と降温結晶化温度(Tc)の関係が
15≦Tm−Tc<25    (℃)であり、かつ球
晶サイズが30μm以下の大きさであることを特徴とす
るオキシメチレン多元共重合体。
Claim 1: (a) trioxane and (b) at least one member selected from ethylene oxide, 1,3-dioxolane, 1,3-dioxepane, 1,3,5-trioxepane, and 1,3,6-trioxocane. An oxymethylene multi-component copolymer obtained by copolymerizing a cyclic ether compound and (c) at least one compound selected from glycidyl phenyl ether, styrene oxide, and glycidyl naphthyl ether, the oxymethylene multi-component copolymer An oxymethylene multicomponent compound characterized in that the relationship between the melting point (Tm) and cooling crystallization temperature (Tc) is 15≦Tm-Tc<25 (°C) and the spherulite size is 30 μm or less. Polymer.
JP03028672A 1991-02-22 1991-02-22 Oxymethylene multi-component copolymer Expired - Lifetime JP3109104B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03028672A JP3109104B2 (en) 1991-02-22 1991-02-22 Oxymethylene multi-component copolymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03028672A JP3109104B2 (en) 1991-02-22 1991-02-22 Oxymethylene multi-component copolymer

Publications (2)

Publication Number Publication Date
JPH04266917A true JPH04266917A (en) 1992-09-22
JP3109104B2 JP3109104B2 (en) 2000-11-13

Family

ID=12254997

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03028672A Expired - Lifetime JP3109104B2 (en) 1991-02-22 1991-02-22 Oxymethylene multi-component copolymer

Country Status (1)

Country Link
JP (1) JP3109104B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1053679C (en) * 1994-02-28 2000-06-21 旭化成工业株式会社 Process for producing acetal copolymer
WO2000055227A1 (en) * 1999-03-15 2000-09-21 Polyplastics Co., Ltd. Polyacetal copolymer and method for producing the same
US6255440B1 (en) 1998-07-24 2001-07-03 Polyplastics Co., Ltd. Copolyacetal
EP1273624A1 (en) * 1999-12-02 2003-01-08 Polyplastics Co. Ltd. Branched polyacetal resin composition
CN1105127C (en) * 1996-09-30 2003-04-09 汎塑料株式会社 Process for producing stabilized oxymethylene copolymer
JP2010265467A (en) * 1999-09-13 2010-11-25 Asahi Kasei Chemicals Corp Method of producing polyacetal copolymer
JP2019052212A (en) * 2017-09-13 2019-04-04 旭化成株式会社 Resin composition and resin molding
WO2023171316A1 (en) * 2022-03-11 2023-09-14 ポリプラスチックス株式会社 Polyacetal copolymer and method for polymerizing same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0649946U (en) * 1992-09-29 1994-07-08 帝国ピストンリング株式会社 Stylus-type profiler

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1053679C (en) * 1994-02-28 2000-06-21 旭化成工业株式会社 Process for producing acetal copolymer
CN1105127C (en) * 1996-09-30 2003-04-09 汎塑料株式会社 Process for producing stabilized oxymethylene copolymer
US6255440B1 (en) 1998-07-24 2001-07-03 Polyplastics Co., Ltd. Copolyacetal
WO2000055227A1 (en) * 1999-03-15 2000-09-21 Polyplastics Co., Ltd. Polyacetal copolymer and method for producing the same
US6426393B1 (en) 1999-03-15 2002-07-30 Polyplastics Co., Ltd. Polyacetal copolymer and method for producing the same
JP2010265467A (en) * 1999-09-13 2010-11-25 Asahi Kasei Chemicals Corp Method of producing polyacetal copolymer
EP1273624A1 (en) * 1999-12-02 2003-01-08 Polyplastics Co. Ltd. Branched polyacetal resin composition
EP1273624A4 (en) * 1999-12-02 2005-11-02 Polyplastics Co Branched polyacetal resin composition
JP2019052212A (en) * 2017-09-13 2019-04-04 旭化成株式会社 Resin composition and resin molding
WO2023171316A1 (en) * 2022-03-11 2023-09-14 ポリプラスチックス株式会社 Polyacetal copolymer and method for polymerizing same

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