JPH09118822A - Polyamide composition - Google Patents

Polyamide composition

Info

Publication number
JPH09118822A
JPH09118822A JP29881695A JP29881695A JPH09118822A JP H09118822 A JPH09118822 A JP H09118822A JP 29881695 A JP29881695 A JP 29881695A JP 29881695 A JP29881695 A JP 29881695A JP H09118822 A JPH09118822 A JP H09118822A
Authority
JP
Japan
Prior art keywords
wax
weight
caprolactam
parts
modified
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
JP29881695A
Other languages
Japanese (ja)
Other versions
JP3419975B2 (en
Inventor
Junji Asano
順治 浅野
Masaaki Hiramoto
雅明 平本
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.)
NIPPON PORIPENKO KK
Original Assignee
NIPPON PORIPENKO KK
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 NIPPON PORIPENKO KK filed Critical NIPPON PORIPENKO KK
Priority to JP29881695A priority Critical patent/JP3419975B2/en
Publication of JPH09118822A publication Critical patent/JPH09118822A/en
Application granted granted Critical
Publication of JP3419975B2 publication Critical patent/JP3419975B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain the subject composition having lubricating properties by blending a poly-ε-caprolactam with a polyethylene wax and a modified polyethylene wax to uniformly disperse the blend. SOLUTION: This polyamide composition is obtained by blending (A) 100 pts.wt. of a poly-ε-caprolactam with (B) 1-12 pts.wt. of a polyethylene wax and (C) 0.1-5 pts.wt. of a modified polyethylene wax containing a hydroxyl group or an epoxide group at the end and/or side chain. For example, preferably the component B and the component C are added to (D) anhydrous ε- caprolactam and heated in the presence of an anionic polymerization derivative and a polymerization cocatalyst at a temperature equal to or higher than the melting point of the component D and equal to or lower than the melting point of the component A (generally 130-180 deg.C) to subject the component D to anionic polymerization.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明はポリアミド組成
物、特にポリアミド樹脂にワックスを均一に分散、配合
してなる潤滑性を有するモノマ−キャストナイロン組成
物に係わるものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyamide composition, and more particularly to a monomer-cast nylon composition having a lubricity obtained by uniformly dispersing and blending a wax in a polyamide resin.

【0002】[0002]

【従来の技術】ポリアミド、特にモノマ−キャストナイ
ロンは摺動性を有しており、無潤滑剤状態にて摺動材料
として用いられるが高速、高荷重等の条件下ではポリア
ミド自体の有する潤滑性では不十分となるため、滑剤を
添加することが提案されている。この滑剤としてはワッ
クス等が使用されている。
2. Description of the Related Art Polyamides, especially monomer-cast nylons, have a sliding property and are used as a sliding material in a lubricant-free state, but under the conditions of high speed, high load, etc., the polyamide itself has a lubricating property. Since it is not enough, it is proposed to add a lubricant. Wax or the like is used as the lubricant.

【0003】[0003]

【発明が解決しようとする課題】滑剤としてワックスを
使用すると、ε−カプロラクタムをアニオン重合させ、
ポリアミド樹脂を得る際に溶融しているε−カプロラク
タムと滑剤が比重の差や非溶融性であるために分離を起
こし、滑剤の分散が不均一になる場合がある。滑剤の分
散が不均一になった場合、製品単体内において、潤滑性
の程度が部分的に不均一になったり、或いは外観の異な
る部位を発生したりする。また、同品種の製品同士の間
でも潤滑性の度合いにばらつきが生じたり、或いは外観
の異なる製品が発生したりする。さらに、滑剤の分離が
容易に起ってしまうので、成形条件が制約される不都合
も起る。
When wax is used as a lubricant, ε-caprolactam is anionically polymerized,
When the polyamide resin is obtained, the molten ε-caprolactam and the lubricant may be separated due to the difference in specific gravity and the non-melting property, and the lubricant may be dispersed unevenly. When the dispersion of the lubricant becomes non-uniform, the degree of lubricity becomes partially non-uniform within the product itself, or a site having a different appearance is generated. Further, the degree of lubricity may vary among products of the same type, or products with different appearances may occur. Further, since the lubricant is easily separated, the molding conditions are restricted.

【0004】[0004]

【課題を解決するための手段】本発明者等は上記従来の
問題点を解消し、滑剤を均一に分散、配合してなるポリ
アミド組成物を得ることを目的として検討を重ね、この
目的を達成する本発明に到達した。即ち、本発明の要旨
とするところは、ポリ−ε−カプロラクタム100 重量部
に、ポリエチレンワックスを1 〜12重量部並びに末端及
び/又は側鎖に水酸基又はエポキシド基を有する変性ポ
リエチレンワックスを0.1 〜5 重量部の割合で分散、配
合してなるポリアミド組成物に存する。
[Means for Solving the Problems] The inventors of the present invention have made extensive studies to solve the above-mentioned problems of the prior art and to obtain a polyamide composition obtained by uniformly dispersing and blending a lubricant, and achieved this object. The present invention has been reached. That is, the gist of the present invention is that 100 parts by weight of poly-ε-caprolactam, 1 to 12 parts by weight of polyethylene wax and 0.1 to 5 parts of modified polyethylene wax having a hydroxyl group or an epoxide group at the terminal and / or side chains. It exists in a polyamide composition obtained by dispersing and blending in a proportion of parts by weight.

【0005】[0005]

【発明の実施の形態】本発明で用いられるポリエチレン
ワックス(以下、これをPEワックスと略称する)は分
子量800 〜12000 のように、比較的低分子量であり、融
点は通常90〜140 ℃であって、例えばエチレンを重合し
てポリエチレンを製造する際の副生品として、又はエチ
レンの分解或いは直接重合等によって得られる。
BEST MODE FOR CARRYING OUT THE INVENTION The polyethylene wax used in the present invention (hereinafter abbreviated as PE wax) has a relatively low molecular weight such as a molecular weight of 800 to 12000, and its melting point is usually 90 to 140 ° C. For example, it is obtained as a by-product when ethylene is polymerized to produce polyethylene, or by decomposition of ethylene or direct polymerization.

【0006】本発明で用いられる水酸基又はエポキシド
基を末端及び/又は側鎖に有する変性ポリエチレンワッ
クス(以下、変性ポリエチレンワックスを変性PEワッ
クスと略称することがある)は分子量が800 〜12000 程
度、融点が通常90〜140 ℃のものである。これらの極性
基を有する変性PEワックスを製造するには、従来から
極性基導入付加方法として知られている手法に準じて行
なえばよい。例えば水酸基の付加には、PEワックスに
対し、一旦その末端をエチレンオキサイドで置換し、そ
れを更に水酸基に変える。またエポキシド基の付加は、
例えば過酢酸の処理による。これらの方法によって得ら
れたPEワックスの末端ないし側鎖に1〜3 個程度の水
酸基又はエポキシド基を有するものが使用される。
The modified polyethylene wax having a hydroxyl group or an epoxide group at the terminal and / or side chain used in the present invention (hereinafter, the modified polyethylene wax may be abbreviated as modified PE wax) has a molecular weight of about 800 to 12000 and a melting point. Is usually 90 to 140 ° C. The modified PE wax having these polar groups may be produced according to a method conventionally known as a polar group introduction / addition method. For example, to add a hydroxyl group, the end of PE wax is once replaced with ethylene oxide, and then it is further converted into a hydroxyl group. The addition of the epoxide group is
For example by treatment with peracetic acid. The PE wax obtained by these methods has about 1 to 3 hydroxyl groups or epoxide groups at the terminal or side chain.

【0007】本発明において、PEワックスの配合割合
は、ポリ−ε−カプロラクタム100重量部に対し、1 〜1
2重量部、好ましくは2 〜6 重量部である。この割合が1
重量部未満であると潤滑効果が乏しく、一方12重量部
を越えると、組成物の機械的強度が低下し、エンジニア
リングプラスチックとして好ましくない。本発明におい
て、末端及び/又は側鎖に水酸基又はエポキシド基を有
する変性PEワックスの配合割合はポリ−ε−カプロラ
クタム100 重量部に対し、0.1 〜5 重量部、好ましくは
0.3 〜3 重量部である。この割合が0.1 重量部未満であ
ると潤滑剤の分散効果が乏しく、一方5 重量部を越える
と、ε−カプロラクタムの重合が阻害される徴候を表わ
し、組成物の機械的強度が低下する。
In the present invention, the blending ratio of PE wax is 1 to 1 with respect to 100 parts by weight of poly-ε-caprolactam.
It is 2 parts by weight, preferably 2 to 6 parts by weight. This ratio is 1
If it is less than 10 parts by weight, the lubricating effect is poor, while if it exceeds 12 parts by weight, the mechanical strength of the composition decreases, which is not preferable as an engineering plastic. In the present invention, the proportion of the modified PE wax having a hydroxyl group or an epoxide group at the terminal and / or side chain is 0.1 to 5 parts by weight, preferably 100 parts by weight of poly-ε-caprolactam.
0.3 to 3 parts by weight. If this proportion is less than 0.1 parts by weight, the effect of dispersing the lubricant will be poor, while if it exceeds 5 parts by weight, the polymerization of ε-caprolactam will be impaired, and the mechanical strength of the composition will decrease.

【0008】本発明で配合する変性PEワックスは末端
及び/又は側鎖に水酸基を有するもの、また末端及び/
又は側鎖にエポキシド基を有するものを単独で或いは両
方を併せて配合してもよく、もしくはこれらの配合に加
えて、その他の極性基、例えばカルボキシル基を有する
変性PEワックスを加えてもよい。そして変性PEワッ
クスは一方の末端(又は側鎖)に水酸基、エポキシド基
の極性基を有するものであればよく、他方の末端(又は
側鎖)に別の極性基があるものでもよい。
The modified PE wax to be blended in the present invention has a hydroxyl group at the terminal and / or side chain, and also at the terminal and / or
Alternatively, those having an epoxide group in the side chain may be blended alone or in combination of both, or in addition to these blends, a modified PE wax having another polar group such as a carboxyl group may be added. The modified PE wax may be one having a polar group such as a hydroxyl group or an epoxide group at one end (or side chain), and may have another polar group at the other end (or side chain).

【0009】本発明の組成物は、従来から知られている
アニオン重合法により製造することができる。即ち無水
のε−カプロラクタムにPEワックス及び上記の変性P
Eワックスを加え、アニオン重合触媒及び重合助触媒の
存在下でε−カプロラクタムの融点以上、ポリε−カプ
ロラクタムの融点以下(通常130 〜180 ℃)に加熱して
ε−カプロラクタムをアニオン重合させる。重合触媒及
び重合助触媒は通常用いられているものでよく、重合触
媒としては、例えばアルカリ金属、アルカリ土類金属又
はこれらの金属の水素化物、水酸化物、酸化物等、また
重合助触媒としては、例えばイソシアネ−ト類、トリア
ジン類、置換尿素類を、通常0.05〜2 モル%の範囲内で
用いる。
The composition of the present invention can be produced by a conventionally known anionic polymerization method. That is, anhydrous ε-caprolactam was added to PE wax and the above-mentioned modified P.
E wax is added and heated to a temperature not lower than the melting point of ε-caprolactam and not higher than the melting point of poly ε-caprolactam (usually 130 to 180 ° C.) in the presence of an anionic polymerization catalyst and a polymerization promoter to anionicly polymerize ε-caprolactam. The polymerization catalyst and the polymerization co-catalyst may be those usually used, and examples of the polymerization catalyst include alkali metals, alkaline earth metals or hydrides of these metals, hydroxides, oxides, and the like. For example, isocyanates, triazines and substituted ureas are usually used within the range of 0.05 to 2 mol%.

【0010】[0010]

【実施例】次に本発明の実施例及びこれと対比するため
の比較例を示すが、本発明は下記実施例によって制限さ
れるものでない。以下の実施例及び比較例では、それぞ
れの組成物について、限界PV値(単位はkg/cm2 ・m
/分)及び引張強度(kg /cm2)を測定した。限界PV値
は潤滑性及び耐摩耗性の評価を示すものであり、この値
は東洋ボ−ルドウイン社製 鈴木式摩耗、摩擦試験機に
より、ポリアミド成形品とS−45C鋼を面圧(P)50
(kg/cm2)毎に加重し、かつ摩擦速度(V)5(m/分)で
摩擦させ、3 分間異常摩耗を起さないPVの最大値を示
す。組成物を成形するための金型の形状、寸法は、内径
50 mm 、長さ1200 mm の鉄の筒に底蓋をしたもので、垂
直に設置される。引張強度は、ASTM規格のD-638 法を常
温で行なって得られた値である。
EXAMPLES Examples of the present invention and comparative examples for comparison will be shown below, but the present invention is not limited to the following examples. In the following examples and comparative examples, for each composition, the limit PV value (unit is kg / cm 2 · m
/ Min) and tensile strength (kg / cm 2 ) were measured. The limit PV value indicates the evaluation of lubricity and wear resistance, and this value is a surface pressure (P) of a polyamide molded product and S-45C steel by a Suzuki type wear and friction tester manufactured by Toyo Ballwind Co., Ltd. 50
The maximum value of PV that does not cause abnormal wear for 3 minutes is shown, which is weighted for each (kg / cm 2 ), and rubbed at a friction speed (V) of 5 (m / min). The shape and size of the mold for molding the composition is the inner diameter
A 50 mm, 1200 mm long steel tube with a bottom lid, installed vertically. The tensile strength is a value obtained by performing the ASTM standard D-638 method at room temperature.

【0011】実施例1〜11及び比較例1〜6 ステンレス鋼製ビ−カ−に無水のε−カプロラクタム50
重量部を採り、160 ℃に調整する。これに重合助触媒の
トリレンジイソシアネ−ト0.5 重量部を加え、更に予め
溶融しておいたPEワックス (分子量4000、融点132
℃) 及びPEワックスの分子片末端に又は側鎖に1 〜3
個の水酸基又はエポキシド基を導入した変性ワックス
を、後記表1に記載した種々の重量部の割合で加え均一
に撹拌する。別のステンレス鋼製ビ−カ−に無水のε−
カプロラクタム50重量部を採り、これに重合触媒の水素
化ナトリウム (油性63%)0.2重量部を加え150 ℃に調整
する。これを上記のPEワックス等を含有する混合物と
混合し、その系を均一にした後、160 ℃の金型に注入
し、潤滑剤などが分散したポリε−カプロラクタム組成
物の円柱状成形品を得た。
Examples 1 to 11 and Comparative Examples 1 to 6 Stainless steel beaker with anhydrous ε-caprolactam 50
Take part by weight and adjust to 160 ° C. To this, 0.5 part by weight of tolylene diisocyanate as a polymerization co-catalyst was added, and further pre-melted PE wax (molecular weight 4000, melting point 132
1 to 3 at the end of one side of PE wax or at the side chain.
The modified wax having individual hydroxyl groups or epoxide groups introduced is added at a ratio of various parts by weight shown in Table 1 below and stirred uniformly. Anhydrous ε-in another stainless steel beaker
Take 50 parts by weight of caprolactam, and add 0.2 parts by weight of sodium hydride (63% oily) as a polymerization catalyst to 150 ℃. This was mixed with a mixture containing the above PE wax and the like to homogenize the system, and then the mixture was poured into a mold at 160 ° C. to obtain a cylindrical molded article of a poly ε-caprolactam composition in which a lubricant and the like were dispersed. Obtained.

【0012】得られたポリε−カプロラクタム組成物に
おいて、このものの製造に当って配合したPEワックス
の量 (重量部) 及び変性PEワックスについては水酸基
を有するものとエポキシド基を有するものとに分けて、
それぞれの配合量 (重量部)並びに得られた組成物の成
形品の上部 (成形品の上方から50 mm の部位) 及び下部
(成形品の下方から30 mm の部位) の限界PV値 (単位
はkg/cm2 ・m /分)及び引張強度 (単位kg/cm2)を表
1に示す。表中、実1は実施例1、比1は比較例1を表
わし、以下同様に表示する。
In the obtained poly ε-caprolactam composition, the amount of PE wax (part by weight) blended in the production of the poly (ε-caprolactam) and the modified PE wax are divided into those having a hydroxyl group and those having an epoxide group. ,
Each compounding amount (part by weight) and the upper part (50 mm from the upper part of the molded product) and the lower part of the molded product of the obtained composition
Table 1 shows the limiting PV value (unit: kg / cm 2 · m / min) and tensile strength (unit: kg / cm 2 ) of (30 mm from the bottom of the molded product). In the table, Ex 1 indicates Example 1 and Ratio 1 indicates Comparative Example 1, which will be referred to hereinafter.

【0013】[0013]

【表1】 [Table 1]

【0014】実施例12〜14及び比較例7〜12 100 C.C.容量のガラス製メスシリンダ−に予め160 ℃に
調整しておいたε−カプロラクタム100 重量部を採り、
これに予め160 ℃に調整しておいたPEワックス (分子
量4000、融点132 ℃) 及びPEワックスの分子片末端及
び/又は側鎖に1 〜3 個の水酸基又はエポキシド基を導
入した変性PEワックスを後記表2に記載した種々の重
量部の割合で加え、密栓をした後、完全に均一に混合す
るために20秒間震動させた後、160 ℃のオ−ブン内で10
分間靜置した直後に、分離したPEワックス及び変性P
Eワックスの両者混合物 (以下の表2では総PEワック
スと記す) の分離量 (重量部) を表2に示す。
Examples 12 to 14 and Comparative Examples 7 to 12 100 parts by weight of ε-caprolactam preliminarily adjusted to 160 ° C. was taken in a glass graduated cylinder having a capacity of 100 CC.
PE wax (molecular weight 4000, melting point 132 ° C.) previously adjusted to 160 ° C. and modified PE wax in which 1 to 3 hydroxyl groups or epoxide groups were introduced into one end and / or side chain of the PE wax were added. The mixture was added at various parts by weight shown in Table 2 below, sealed, and shaken for 20 seconds to mix thoroughly, and then heated in an oven at 160 ° C for 10 seconds.
Immediately after standing for a minute, the separated PE wax and modified P
Table 2 shows the separated amount (parts by weight) of the mixture of both E waxes (referred to as total PE wax in Table 2 below).

【0015】[0015]

【表2】 [Table 2]

【0016】上記表2における例は、何れも本発明組成
物を製造する途中で採取した総PEワックス量を対比す
るものであるが、上記結果から、本発明に規定する組成
割合によれば総PEワックスの分離量が0 であるのに対
し、本発明外の割合では総PEワックスの分離量が多
く、かかる配合割合によれば、得られた組成物において
物性が不均一で好ましくないことは自明といえる。な
お、比較例12は、変性PEワックスが多量に配合され
ても、分離を起すことがないことを参考的に示すもので
ある。なお、表2において、実12は実施例12、比7
は比較例7を表わし、以下同様に表示する。
The examples in Table 2 above all compare the total amount of PE wax collected during the production of the composition of the present invention. The separation amount of the PE wax is 0, whereas the separation amount of the total PE wax is large at the ratios outside the present invention. According to such a mixing ratio, the physical properties of the obtained composition are not uniform, which is not preferable. It can be called obvious. It should be noted that Comparative Example 12 is a reference example showing that no separation occurs even if a large amount of modified PE wax is blended. In addition, in Table 2, Ex. 12 is Example 12 and ratio 7
Represents Comparative Example 7, and is similarly displayed below.

【0017】本発明の実施態様例を挙げると次の通りで
ある。 (1) モノマ−キャスティング法によって製造されたもの
であって、ポリ−ε−カプロラクタム100 重量部に、P
Eワックスを1 〜12重量部並びに末端及び/又は側鎖に
水酸基又はエポキシド基を有する変性PEワックスを0.
1 〜5 重量部の割合で分散、配合してなるポリアミド組
成物。 (2) 配合するPEワックスは分子量が800 〜12000 であ
るポリアミド組成物。 (3) 配合するPEワックスは融点が90〜140 ℃であるポ
リアミド組成物。 (4) 配合する変性PEワックスは分子量が800 〜12000
であるポリアミド組成物。 (5) 配合する変性PEワックスは融点が90〜140 ℃であ
るポリアミド組成物。
An example of the embodiment of the present invention is as follows. (1) A polymer produced by a monomer casting method, wherein 100 parts by weight of poly-ε-caprolactam and P
1 to 12 parts by weight of E wax and 0. modified PE wax having a hydroxyl group or an epoxide group at the terminal and / or side chain.
A polyamide composition prepared by dispersing and blending at a ratio of 1 to 5 parts by weight. (2) A polyamide composition in which the PE wax to be blended has a molecular weight of 800 to 12000. (3) A polyamide composition in which the PE wax to be blended has a melting point of 90 to 140 ° C. (4) The modified PE wax to be blended has a molecular weight of 800 to 12000.
A polyamide composition. (5) A polyamide composition in which the modified PE wax to be blended has a melting point of 90 to 140 ° C.

【0018】[0018]

【発明の効果】本発明によれば、単独では分散困難なP
Eワックスに末端及び/又は側鎖に水酸基又はエポキシ
ド基を有する変性PEワックスを併せ配合することによ
り、上記配合物を均一に分散させたポリアミド組成物が
得られる。
According to the present invention, it is difficult to disperse P by itself.
By blending E wax with a modified PE wax having a hydroxyl group or an epoxide group at the terminal and / or side chain, a polyamide composition in which the above blend is uniformly dispersed can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポリ−ε−カプロラクタム100重量部
に、ポリエチレンワックスを1〜12重量部並びに末端
及び/又は側鎖に水酸基又はエポキシド基を有する変性
ポリエチレンワックスを0.1〜5重量部の割合で分
散、配合してなるポリアミド組成物。
1. A ratio of 1 to 12 parts by weight of polyethylene wax and 0.1 to 5 parts by weight of modified polyethylene wax having a hydroxyl group or an epoxide group at the terminal and / or side chain per 100 parts by weight of poly-ε-caprolactam. A polyamide composition prepared by dispersing and blending with.
JP29881695A 1995-10-24 1995-10-24 Monomer cast nylon molded from polyamide composition Expired - Fee Related JP3419975B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29881695A JP3419975B2 (en) 1995-10-24 1995-10-24 Monomer cast nylon molded from polyamide composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29881695A JP3419975B2 (en) 1995-10-24 1995-10-24 Monomer cast nylon molded from polyamide composition

Publications (2)

Publication Number Publication Date
JPH09118822A true JPH09118822A (en) 1997-05-06
JP3419975B2 JP3419975B2 (en) 2003-06-23

Family

ID=17864596

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29881695A Expired - Fee Related JP3419975B2 (en) 1995-10-24 1995-10-24 Monomer cast nylon molded from polyamide composition

Country Status (1)

Country Link
JP (1) JP3419975B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009292910A (en) * 2008-06-04 2009-12-17 Mitsui Chemicals Inc Resin composition for molding blended with inorganic reinforcement

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100816068B1 (en) 2007-04-10 2008-03-24 주식회사 에스앤엠 Manufacturing methods of auti-fire mc nylon and anti-fire mc nylon thereof
KR100795171B1 (en) 2007-04-10 2008-01-16 주식회사 에스앤엠 Manufacturing methods of conductine mc nylon and conductine mc nylon thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009292910A (en) * 2008-06-04 2009-12-17 Mitsui Chemicals Inc Resin composition for molding blended with inorganic reinforcement

Also Published As

Publication number Publication date
JP3419975B2 (en) 2003-06-23

Similar Documents

Publication Publication Date Title
US4035438A (en) Impact resistant polymer mixtures
JPS6320254B2 (en)
EP2520603B1 (en) Composition for anionic lactam polymerisation, process for it production and use
JP7227425B2 (en) Branch-terminated polyamide composition
US3442975A (en) Polyimine/polycarbonamide graft polymers
US3036988A (en) Homogeneous blend of a polyamide and a polyvinyl lactam and process for producing
US3252905A (en) Polyamide bearings
JPH09118822A (en) Polyamide composition
US3770689A (en) Process for the anionic catalytic polymerization of lactams
CA1303782C (en) Process for the anionic polymerization of caprolactam, and for the copolymerization thereof with other lactams
JP2024509187A (en) High flow double end-capped polyamide polymer
Haba et al. Development and characterization of reactively extruded PVC/polystyrene blends
JP3015206B2 (en) Polyamide composition
JP3736909B2 (en) Resin composition with excellent slidability
JP3419967B2 (en) Polyamide composition
US4581191A (en) Method for the production of molded articles from polylaurolactam, as well as the resulting molded articles
US4362862A (en) Preparation of poly-2-pyrrolidone with N-(2-caprolactim)-caprolactam accelerator
JP2001002781A (en) Production of polyamide pellet and polyamide fiber and molded article
NZ757619B2 (en) Branched, terminated polyamide compositions
AU2021221961A1 (en) Polyamide-based masterbatch formulation
JPS60223822A (en) Production of filled polyamide
KR20000018763A (en) Method for producing polyester recycled fiber
JP2002030148A (en) Polyamide resin composition and fiber
CN108659518A (en) The manufacturing method of resin particle and its manufacturing method and molded product
DE1669371A1 (en) Polyamide mixture for the production of threads and fibers

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20030401

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090418

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees