JPH1067023A - Manufacture of casting polyamide resin molded object - Google Patents
Manufacture of casting polyamide resin molded objectInfo
- Publication number
- JPH1067023A JPH1067023A JP24555496A JP24555496A JPH1067023A JP H1067023 A JPH1067023 A JP H1067023A JP 24555496 A JP24555496 A JP 24555496A JP 24555496 A JP24555496 A JP 24555496A JP H1067023 A JPH1067023 A JP H1067023A
- Authority
- JP
- Japan
- Prior art keywords
- mold
- lactam
- liquid
- liquid paraffin
- film
- 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
Links
Landscapes
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は注型ポリアミド樹脂
成形体の製造方法に係り、詳しくは上部層に気泡のよう
な空洞欠陥のない注型ポリアミド樹脂成形体で、特に丸
棒、角棒のような棒状成形体を製造するのに有効な注型
ポリアミド樹脂成形体の製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a cast polyamide resin molded article, and more particularly to a cast polyamide resin molded article having no voids such as air bubbles in an upper layer. The present invention relates to a method for producing a cast polyamide resin molded article effective for producing such a rod-shaped molded article.
【0002】[0002]
【従来の技術】注型ポリアミド棒状成形体の製造方法
は、筒状体の金型を熱風炉で所定の温度になるまで加熱
しておき、この金型を炉から取り出して重合性ラクタム
液をこれに注入し、再び金型を熱風炉に入れてラクタム
を重合していた。得られた注型ポリアミド棒状成形体は
最も代表的なエンジニアリングプラスチックであり、機
械的強さ、耐衝撃性、耐熱性、耐薬品性に優れ、しかも
成形性もよいため、ギヤー、ロール、摺動板などの多く
の機械部品として使用されている。2. Description of the Related Art In a method of manufacturing a cast polyamide rod-shaped molded body, a cylindrical mold is heated to a predetermined temperature in a hot blast stove, and the mold is removed from the furnace to remove a polymerizable lactam liquid. The lactam was injected into the mold, and the mold was placed in a hot-blast furnace again to polymerize the lactam. The obtained cast polyamide rod-shaped molded product is the most representative engineering plastic, and has excellent mechanical strength, impact resistance, heat resistance, chemical resistance, and good moldability. Used as many mechanical parts such as boards.
【0003】しかし、この方法によると、金型に注入し
た重合性ラクタム液が空気に接しているため、内部層と
上部層との温度差による重合収縮の差、空気中の水分に
よる重合阻害、あるいは重合性ラクタム液の酸化劣化が
発生することにより棒状体上部に空洞部や流れ模様が多
発し、止むを得ず棒状体上部を所定長さに切断し、製品
として出荷していた。このため、従来では金型に注入し
た重合性ラクタム液に接する空気層を加熱した窒素で置
換するなどの方法が採用されてきた。However, according to this method, since the polymerizable lactam liquid injected into the mold is in contact with air, the difference in polymerization shrinkage due to the temperature difference between the inner layer and the upper layer, the inhibition of polymerization due to moisture in the air, Alternatively, the oxidative deterioration of the polymerizable lactam liquid causes cavities and flow patterns to occur frequently on the upper part of the rod-shaped body, and the upper part of the rod-shaped body is unavoidably cut to a predetermined length and shipped as a product. For this reason, conventionally, a method of replacing the air layer in contact with the polymerizable lactam liquid injected into the mold with heated nitrogen has been adopted.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、重合性
ラクタム液はその重合過程において体積が変化するため
金型の蓋を密閉できないことにより、上記方法では窒素
置換の十分な効果が得られなかった。また、重合過程
中、継続して金型中に加熱窒素を送り続ける方法も提案
されたが、設備費用が高くなり、経済性の点で問題があ
った。本発明はこのような問題点を改善するものであ
り、重合性ラクタム液の重合過程の特性を充分に考慮す
ることにより、上部層に気泡のような空洞欠陥及び流れ
模様のない注型ポリアミド樹脂成形体を得ることができ
る製造方法を提供することにある。However, since the volume of the polymerizable lactam liquid changes during the polymerization process, the mold lid cannot be closed, and thus the above method cannot provide a sufficient effect of nitrogen replacement. Further, a method has been proposed in which heated nitrogen is continuously fed into the mold during the polymerization process. However, equipment costs are increased and there is a problem in terms of economic efficiency. The present invention has been made to solve such problems, and by fully considering the characteristics of the polymerization process of the polymerizable lactam liquid, a cast polyamide resin free of void defects such as air bubbles and a flow pattern in an upper layer. An object of the present invention is to provide a manufacturing method capable of obtaining a molded body.
【0005】[0005]
【課題を解決するための手段】即ち、本願の請求項1の
発明は、実質上無水のω−ラクタムに少なくともアニオ
ン重合触媒とアニオン重合用開始剤とからなる重合性ラ
クタム液を金型内でアニオン重合するにおいて、金型内
へ注入した重合性ラクタム液の表面に流動パラフィンを
滴下して膜を形成した後、重合を進行させる注型ポリア
ミド樹脂成形体の製造方法にあり、特に流動パラフィン
の膜を形成した後、重合することにより、成形体の上部
層に空洞部や流れ模様を阻止することができた。That is, the invention of claim 1 of the present application provides a substantially anhydrous ω-lactam with a polymerizable lactam liquid comprising at least an anionic polymerization catalyst and an anionic polymerization initiator in a mold. In the anionic polymerization, after forming a film by dropping liquid paraffin on the surface of the polymerizable lactam liquid injected into the mold, there is a method for producing a cast polyamide resin molded body in which the polymerization proceeds, particularly the liquid paraffin After the film was formed, polymerization was carried out, whereby a cavity and a flow pattern could be prevented in the upper layer of the molded article.
【0006】本願の請求項2の発明は、流動パラフィン
の膜厚を0.2〜5.0mmにすることにより、金型に
注入した重合性ラクタム液を保温し、空気を遮断するこ
とにより比較的均一に重合することができ、より確実に
上部層に気泡のような空洞欠陥のない注型ポリアミド樹
脂成形体を得ることができる。According to the invention of claim 2 of the present application, the thickness of the liquid paraffin is set to 0.2 to 5.0 mm so that the polymerizable lactam liquid injected into the mold is kept warm and the air is cut off. Polymerization can be carried out uniformly and uniformly, and a cast polyamide resin molded article free of void defects such as air bubbles in the upper layer can be obtained more reliably.
【0007】本願の請求項3の発明は、80〜140°
Cに加熱した流動パラフィンを滴下して膜を形成し、加
熱した流動パラフィン膜と金型に注入した重合性ラクタ
ム液の温度差を小さくすることにより、より確実に上部
層に気泡のような空洞欠陥のない注型ポリアミド樹脂成
形体を得ることができる。[0007] The invention according to claim 3 of the present application is the invention in the range of 80 to 140 °.
C. A liquid paraffin heated to C is dropped to form a film, and the temperature difference between the heated liquid paraffin film and the polymerizable lactam liquid injected into the mold is reduced, so that a cavity like an air bubble is more reliably formed in the upper layer. A cast polyamide resin molded article without defects can be obtained.
【0008】[0008]
【発明の実施の形態】図1は本発明に係る注型ポリアミ
ド樹脂成形体の製造方法に使用する重合装置の概略図で
ある。この装置1では、溶融ラクタムにアニオン重合触
媒を入れた貯蔵タンク2と、溶融ラクタムにアニオン重
合開始剤を入れた貯蔵タンク3とに分かれ、貯蔵タンク
2、3とミキシング4の間には、それぞれバルブ6を装
着した管7が接続されている。各貯蔵タンク2、3から
流出した溶融ラクタムは、ミキシング部4で混合攪拌さ
れた後に、150〜180°Cに加熱されたアルミ、鉄
等の熱伝導率の比較的高い金型5に注型される。DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a schematic view of a polymerization apparatus used in a method for producing a cast polyamide resin molded article according to the present invention. This apparatus 1 is divided into a storage tank 2 in which an anionic polymerization catalyst is put in a molten lactam and a storage tank 3 in which an anion polymerization initiator is put in a molten lactam. A tube 7 equipped with a valve 6 is connected. The molten lactam flowing out of each of the storage tanks 2 and 3 is mixed and stirred in the mixing section 4 and then cast into a mold 5 having a relatively high thermal conductivity such as aluminum or iron heated to 150 to 180 ° C. Is done.
【0009】各貯蔵タンク2、3には、窒素を供給する
管8とこれを排出する管9が設けられ、タンク内の圧力
を常時一定にしている。尚、各貯蔵タンク2、3に設け
たバルブ6の下側に計量ポンプ(図示せず)を設置する
ことができる。A pipe 8 for supplying nitrogen and a pipe 9 for discharging the nitrogen are provided in each of the storage tanks 2 and 3 so that the pressure in the tanks is always kept constant. A metering pump (not shown) can be installed below the valve 6 provided in each of the storage tanks 2 and 3.
【0010】金型5内に重合性ラクタム液を注型した直
後に、図2に示すように金型5の蓋を開け、加熱した所
定量の流動パラフィンを滴下して膜10を形成した後
に、再度蓋をしてこの金型5を雰囲気温度100〜21
0°C、好ましくは130〜180°Cに調節したオー
ブンに入れた後、重合を進行させる。Immediately after casting the polymerizable lactam liquid into the mold 5, the lid of the mold 5 is opened as shown in FIG. 2, and a predetermined amount of heated liquid paraffin is dropped to form the film 10. Then, the mold 5 is closed again and the mold 5 is heated to an ambient temperature of 100 to 21.
After placing in an oven controlled at 0 ° C, preferably 130-180 ° C, the polymerization is allowed to proceed.
【0011】この場合、流動パラフィンは、注型した重
合性ラクタム液の温度に近似させるため80〜140°
Cに加熱して、重合性ラクタム液の表面層の温度を低下
させずに内部温度に維持して表面層と内部層の温度勾配
を小さくし、未反応のモノマーが残存しないようにして
いる。また、流動パラフィンの膜厚も0.2〜5.0m
mに設定する必要がある。膜厚が0.2mm未満では、
断熱膜及び空気遮断膜として効果が小さく、成形体の上
部層に空洞部や流れ模様が多発して成形体の表面層に空
洞部や流れ模様が発生する。一方、膜厚が5.0mmを
越えると、膜厚の効果は期待されず、むしろ経済的に不
利になる。In this case, the liquid paraffin is heated to 80 to 140 ° to approximate the temperature of the castable polymerizable lactam liquid.
By heating to C, the temperature of the surface layer of the polymerizable lactam liquid is maintained at the internal temperature without lowering to reduce the temperature gradient between the surface layer and the internal layer so that unreacted monomers do not remain. Also, the thickness of the liquid paraffin is 0.2 to 5.0 m.
m must be set. If the film thickness is less than 0.2 mm,
The effect is small as a heat insulating film and an air blocking film, and cavities and flow patterns frequently occur in the upper layer of the molded body, and cavities and flow patterns are generated in the surface layer of the molded body. On the other hand, if the film thickness exceeds 5.0 mm, the effect of the film thickness is not expected, and it is rather disadvantageous economically.
【0012】ここで使用する流動パラフィンは、化学的
に不活性な無色、無臭の液状炭化水素の混合物であり、
重合性ラクタム液に溶けないものであり、例えばエッソ
石油社製のクリストール(商品名)が挙げられる。The liquid paraffin used here is a mixture of a chemically inert colorless, odorless liquid hydrocarbon,
It does not dissolve in the polymerizable lactam liquid, and includes, for example, Christol (trade name) manufactured by Esso Oil Co., Ltd.
【0013】上記ω−ラクタムは実質上無水のα−ピペ
リドン、ε−カプロラクタム、ω−ラウロラクタム、あ
るいはこれらの2種以上の混合物であり、工業的に有利
なラクタムはε−カプロラクタムとω−ラウロラクタム
である。The ω-lactam is substantially anhydrous α-piperidone, ε-caprolactam, ω-laurolactam, or a mixture of two or more thereof. Industrially advantageous lactams are ε-caprolactam and ω-laurolactam. Lactam.
【0014】また、本発明で使用するアニオン重合触媒
は、水素化ナトリウム、水素化リチウム、ナトリウム、
カリウム等の公知のω−ラクタムの重合触媒を使用する
ことができ、その添加量はω−ラクタムに対して0.1
〜2.0モル%である。そして、アニオン重合用開始剤
としては、例えばN−アセチル−ε−カプロラクタム、
イソシアネート、ジイソシアネート、尿素誘導体、ウレ
タン、イソシアヌレート誘導体であり、その添加量はω
−ラクタムに対して0.05〜1.0モル%の範囲が好
ましい。Further, the anionic polymerization catalyst used in the present invention includes sodium hydride, lithium hydride, sodium,
Known polymerization catalysts for ω-lactams such as potassium can be used, and the amount added is 0.1 to ω-lactam.
~ 2.0 mol%. And, as the initiator for anionic polymerization, for example, N-acetyl-ε-caprolactam,
Isocyanate, diisocyanate, urea derivative, urethane, isocyanurate derivative,
-A range of 0.05 to 1.0 mol% based on lactam is preferred.
【0015】上記製造方法では、アニオン重合触媒をω
−ラクタムに添加し溶解した後、アニオン重合用開始剤
を注型時または注型後に添加混合する方法、またはアニ
オン重合触媒を含むω−ラクタムとアニオン重合用開始
剤を含むω−ラクタムとを注型時または注型後に添加混
合する方法によって調整する。また、ω−ラクタムの重
合温度は100〜210°Cの温度で実施可能である
が、好ましくは130〜180°Cである。[0015] In the above production method, the anionic polymerization catalyst is ω
A method of adding and mixing an anionic polymerization initiator at or after casting after adding and dissolving to a lactam, or injecting an ω-lactam containing an anionic polymerization catalyst and an ω-lactam containing an anionic polymerization initiator. It is adjusted by a method of adding and mixing at the time of molding or after casting. Further, the polymerization temperature of ω-lactam can be carried out at a temperature of 100 to 210 ° C., preferably 130 to 180 ° C.
【0016】尚、本発明方法を実施するに際して、上記
成分以外に重合を阻害しない油類、ワックス、ステアリ
ン酸亜鉛、ステアリン酸カルシウム等の滑剤や、カーボ
ン繊維、ウオラスナイト等の補強材、ポリビニリデンク
ロライド等の着色剤を添加することも可能である。In carrying out the method of the present invention, other than the above components, oils which do not inhibit polymerization, waxes, lubricants such as zinc stearate, calcium stearate, reinforcing materials such as carbon fiber and wollastonite, polyvinylidene chloride, etc. It is also possible to add a coloring agent.
【0017】[0017]
【実施例】以下、実施例により本発明をより詳細に説明
する。 実施例1〜3、比較例1 実質上無水のε−カプロラクタム8.0kgを100°
Cまで加熱溶融し、これに水素化ナトリウム(63%油
性)16gを添加して反応溶解させた。このラクタム液
を125°Cまで昇温し、トリスフェニルイソシアヌレ
ート7gをすばやく混合した後、これを予め140°C
まで予熱したアルミ製の内寸法90φ、深さ1000m
mの円筒状の金型に流し込んだ。この後、85°Cに加
熱した所定量の流動パラフィンを滴下して0.1mm、
0.2mm、1.0mm、そして5.0mmの種々の厚
さの膜を形成した後、170°Cに調節した炉内で重合
させた。上記金型表面に貼付けた温度センサーにより、
金型表面温度が反応熱により上昇し終えた後、1°C降
下した時に、成形体を金型に入れたままで50°Cに調
節した炉の中へ移した。30分後に成形体を金型から取
り出した。成形体を充分に冷却させた後、成形体の上部
層を観察した結果を表1に示す。The present invention will be described in more detail with reference to the following examples. Examples 1-3, Comparative Example 1 8.0 kg of substantially anhydrous ε-caprolactam was added at 100 °
C, and the mixture was heated and melted, and 16 g of sodium hydride (63% oil-based) was added and dissolved therein. This lactam solution was heated to 125 ° C., and 7 g of trisphenyl isocyanurate was quickly mixed.
Pre-heated aluminum inner dimensions 90φ, depth 1000m
m into a cylindrical mold. Thereafter, a predetermined amount of liquid paraffin heated to 85 ° C. was dropped into 0.1 mm,
After forming films of various thicknesses of 0.2 mm, 1.0 mm and 5.0 mm, they were polymerized in a furnace adjusted to 170 ° C. By the temperature sensor stuck on the mold surface,
When the mold surface temperature was lowered by 1 ° C. after the rise in the reaction heat, the molded body was transferred into a furnace adjusted to 50 ° C. while being kept in the mold. After 30 minutes, the compact was removed from the mold. Table 1 shows the results of observation of the upper layer of the molded article after the molded article was sufficiently cooled.
【0018】[0018]
【表1】 [Table 1]
【0019】この結果、流動パラフィンの膜厚が0.2
mm、1.0mm、5.0mmでは、成形体の上部層に
空洞部や流れ模様が認められなかったが、0.1mmで
は成形体の上部層に空洞部や流れ模様が認められた。As a result, the thickness of the liquid paraffin was 0.2
At 1.0 mm, 1.0 mm, and 5.0 mm, no cavity or flow pattern was observed in the upper layer of the molded body, but at 0.1 mm, a cavity or flow pattern was observed in the upper layer of the molded body.
【0020】比較例2 流動パラフィンの代わりに、シリコーンを5.9g滴下
して厚さ1.0mmの膜を形成した後、実施例1と同様
に重合したところ、成形体の上部層に空洞部や流れ模様
が認められた。Comparative Example 2 Instead of liquid paraffin, 5.9 g of silicone was added dropwise to form a 1.0 mm thick film, which was polymerized in the same manner as in Example 1. And flow patterns were observed.
【0021】比較例3 流動パラフィンの代わりに、ポリエチレンワックスを
5.9g滴下して厚さ1.0mmの膜を形成した後、実
施例1と同様に重合したところ、成形体の表面層に空洞
部や流れ模様が認めら、またポリエチレンワックスが成
形体の上部層に溶けているのが観察された。Comparative Example 3 Instead of liquid paraffin, 5.9 g of polyethylene wax was dropped to form a 1.0 mm-thick film, which was polymerized in the same manner as in Example 1. Parts and flow patterns were observed, and it was observed that the polyethylene wax was dissolved in the upper layer of the molded article.
【0022】比較例4 流動パラフィンの代わりに、超高分子量ポリエチレンの
粉末(粒径0.1mm)を落下したとこと、均一な膜が
形成されず、この状態で実施例1と同様に重合したとこ
ろ、成形体の上部層に空洞部や流れ模様が認められた。Comparative Example 4 In place of liquid paraffin, powder of ultra-high molecular weight polyethylene (particle diameter: 0.1 mm) was dropped, and a uniform film was not formed. In this state, polymerization was performed in the same manner as in Example 1. However, cavities and flow patterns were observed in the upper layer of the molded body.
【0023】比較例5 流動パラフィンの代わりに、厚さ0.015mmで金型
の内径に等しい直径をもつ円形のアルミホイールを金型
内へ注入した重合性ラクタム液の表面に設置した後、実
施例1と同様に重合させたところ、成形体の上部層に空
洞部や流れ模様が認められなかったが、上部層の径が小
さくやせていた。以上の実施例1と比較例2〜5の結果
を表2に示す。Comparative Example 5 Instead of liquid paraffin, a circular aluminum wheel having a thickness of 0.015 mm and a diameter equal to the inner diameter of the mold was placed on the surface of the polymerizable lactam liquid injected into the mold, and then the process was carried out. When polymerization was carried out in the same manner as in Example 1, no cavity or flow pattern was observed in the upper layer of the molded product, but the diameter of the upper layer was small and thin. Table 2 shows the results of Example 1 and Comparative Examples 2 to 5 described above.
【0024】[0024]
【表2】 [Table 2]
【0025】この結果より、所定厚さの流動パラフィン
が断熱膜及び空気遮断膜として効果が大きく、成形体の
上部層に空洞部や流れ模様が認められないことが判る。From this result, it can be seen that the liquid paraffin having a predetermined thickness has a large effect as a heat insulating film and an air barrier film, and that no cavity or flow pattern is observed in the upper layer of the molded product.
【0026】[0026]
【発明の効果】以上のように本願の請求項1の発明は、
実質上無水のω−ラクタムに少なくともアニオン重合触
媒とアニオン重合用開始剤とからなる重合性ラクタム液
を金型内でアニオン重合するにおいて、金型内へ注入し
た重合性ラクタム液の表面に流動パラフィンを滴下して
膜を形成した後、重合を進行させる注型ポリアミド樹脂
成形体の製造方法にあり、特に流動パラフィンの膜を形
成した後、重合することにより、成形体の上部層に空洞
部や流れ模様を阻止することができる効果がある。As described above, the invention of claim 1 of the present application is
In anionically polymerizing a polymerizable lactam solution comprising at least an anionic polymerization catalyst and an anionic polymerization initiator onto substantially anhydrous ω-lactam in a mold, liquid paraffin is added to the surface of the polymerizable lactam solution injected into the mold. After forming a film by dropping, a method for producing a cast polyamide resin molded body in which polymerization proceeds is performed.In particular, after forming a film of liquid paraffin, polymerization is performed, so that a cavity or the like is formed in the upper layer of the molded body. There is an effect that the flow pattern can be prevented.
【0027】本願の請求項2の発明は、流動パラフィン
の膜厚を0.2〜5.0mmにすることにより、金型に
注入した重合性ラクタム液を保温して比較的均一に重合
することができ、より確実に上部層に気泡のような空洞
欠陥のない注型ポリアミド樹脂成形体を得ることができ
る効果がある。According to a second aspect of the present invention, a liquid paraffin having a film thickness of 0.2 to 5.0 mm is used to keep the polymerizable lactam liquid injected into the mold warm and relatively uniformly polymerize. Thus, there is an effect that a cast polyamide resin molded article free of void defects such as air bubbles in the upper layer can be more reliably obtained.
【0028】本願の請求項3の発明は、80〜140°
Cに加熱した流動パラフィンを滴下して膜を形成し、加
熱した流動パラフィン膜と金型に注入した重合性ラクタ
ム液の温度差を小さくすることにより、より確実に上部
層に気泡のような空洞欠陥のない注型ポリアミド樹脂成
形体を得ることができる効果がある。[0028] The invention of claim 3 of the present application is the invention in which
C. A liquid paraffin heated to C is dropped to form a film, and the temperature difference between the heated liquid paraffin film and the polymerizable lactam liquid injected into the mold is reduced, so that a cavity like an air bubble is more reliably formed in the upper layer. There is an effect that a cast polyamide resin molded article having no defect can be obtained.
【図1】本発明に係る注型ポリアミド樹脂成形体の製造
方法に使用する重合装置の概略図である。FIG. 1 is a schematic view of a polymerization apparatus used in a method for producing a cast polyamide resin molded article according to the present invention.
【図2】金型内に重合性ラクタム液を注型した後、所定
量の流動パラフィンを滴下して膜を形成した状態を示す
断面図である。FIG. 2 is a cross-sectional view showing a state in which a polymerizable lactam solution is cast into a mold and then a predetermined amount of liquid paraffin is dropped to form a film.
2 貯蔵タンク 3 貯蔵タンク 4 ミキシング 5 金型 10 膜 2 Storage tank 3 Storage tank 4 Mixing 5 Mold 10 Membrane
Claims (3)
アニオン重合触媒とアニオン重合用開始剤とからなる重
合性ラクタム液を金型内でアニオン重合するにおいて、
金型内へ注入した重合性ラクタム液の表面に流動パラフ
ィンを滴下して膜を形成した後、重合を進行させること
を特徴とする注型ポリアミド樹脂成形体の製造方法。1. An anion polymerization in a mold of a polymerizable lactam liquid comprising at least an anionic polymerization catalyst and an anionic polymerization initiator on a substantially anhydrous ω-lactam,
A method for producing a cast polyamide resin article, comprising: forming a film by dropping liquid paraffin on the surface of a polymerizable lactam liquid injected into a mold, and then proceeding with polymerization.
mmである請求項1記載の注型ポリアミド樹脂成形体の
製造方法。2. A liquid paraffin having a film thickness of 0.2 to 5.0.
The method for producing a cast polyamide resin molded article according to claim 1, wherein
ィンを滴下して膜を形成する請求項1または2記載の注
型ポリアミド樹脂成形体の製造方法。3. The method according to claim 1, wherein liquid paraffin heated to 80 to 140 ° C. is dropped to form a film.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24555496A JP3409977B2 (en) | 1996-08-27 | 1996-08-27 | Manufacturing method of cast polyamide resin molded body |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24555496A JP3409977B2 (en) | 1996-08-27 | 1996-08-27 | Manufacturing method of cast polyamide resin molded body |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1067023A true JPH1067023A (en) | 1998-03-10 |
JP3409977B2 JP3409977B2 (en) | 2003-05-26 |
Family
ID=17135436
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24555496A Expired - Fee Related JP3409977B2 (en) | 1996-08-27 | 1996-08-27 | Manufacturing method of cast polyamide resin molded body |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3409977B2 (en) |
-
1996
- 1996-08-27 JP JP24555496A patent/JP3409977B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP3409977B2 (en) | 2003-05-26 |
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