JP3734623B2 - Manufacturing method of polyamide resin molded body - Google Patents

Manufacturing method of polyamide resin molded body Download PDF

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Publication number
JP3734623B2
JP3734623B2 JP19687898A JP19687898A JP3734623B2 JP 3734623 B2 JP3734623 B2 JP 3734623B2 JP 19687898 A JP19687898 A JP 19687898A JP 19687898 A JP19687898 A JP 19687898A JP 3734623 B2 JP3734623 B2 JP 3734623B2
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Japan
Prior art keywords
mold
polymerization
molded body
polyamide resin
lactam
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Expired - Fee Related
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JP19687898A
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Japanese (ja)
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JP2000025051A (en
Inventor
元治 阿部
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日本ポリペンコ株式会社
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【0001】
【発明の属する技術分野】
本発明は、ラクタムのアニオン重合により棒状、板状等の所定形状のポリアミド樹脂成形体の製造方法に係り、特に内部残留気泡がなく、充填材及び補強材等の添加材を添加した際それらが均一に分散した成形体の製造方法に関するものである。
【0002】
【従来の技術】
所定温度に加熱された溶融ラクタムを予め加熱された金型内に注入しアニオン重合させポリアミドを成型する方法では、成形体のサイズや形状により成形体の内部に気泡と呼ばれる空洞欠陥を発生させることが問題となっている。
【0003】
これは成型時の大きな体積収縮に起因するのであり、ラクタム溶液を金型へ注入後重合開始まで、ある程度の時間を要するため重合の進行が各部位でばらついたり、ラクタム溶液を注入後対流が起こり、金型の高さ方向で上部溶液温度が上がり上部より重合することにより発生するのが要因の一つと考えられる。
【0004】
このような内部残留気泡を発生させないために、従来ではラクタム溶液を加圧下で重合する方法が提案されている。また、ラクタム溶液と比重の異なる充填材および補強材等の添加材を添加した場合、重合時に沈降し、均一に分散した成形体が得られ難いという問題に対しては、粒径を細かくしたり、ラクタム液の粘度を上げたりという方法がとられてきた。
【0005】
【発明が解決しようとする課題】
内部残留気泡を無くす従来の方法では成形サイズが大きくなったり、高さ方向で形状の違う成形体を得る場合に応用することが困難であった。さらに、金型を含む成形装置の設備費がかかり経済性の点で問題であった。
【0006】
また、ラクタム溶液に各種添加材を添加した場合、各部位での重合進行速度のばらつきが顕著になり、分散不良に加え内部残留気泡の発生率が高くなり、従来法では両方を押さえることは困難である。
【0007】
【課題を解決するための手段】
本発明は上記のような問題を解決し、成形本体のサイズや形状をを問わず内部残留気泡のないポリアミド樹脂成形体の製造方法に関するものであり、その要旨は、溶融ラクタムをアニオン重合触媒及び助触媒の存在下で、熱検出手段を金型内部の下部、中部及び上部に設けた金型内に注入してポリアミド樹脂成形体を製造する方法であって、金型全体を一定温度に保持した金型内に注入された溶融ラクタムの重合発熱による温度上昇を前記熱検出手段で検出して金型の下部から中部及び上部に順次温度を上昇するように、温度上昇を確認しながら溶融ラクタムの注入速度を調整することを特徴とするポリアミド樹脂成形体の製造方法である。
【0008】
【発明の実施の形態】
以下、本発明を図面に基づき説明する。
【0009】
図1は本発明に使用した成形金型の斜視図であり、高さ600mm、幅1200mm、厚さ20mm、の成形金型1の内部に熱電対2を下部、中部、上部の3個所にセットし金型全体を160℃保持した。
【0010】
本発明において、金型内で重合体の固化を金型の下部から上部に順次進行させる具体的手段、または金型内に於ける重合体の重合発熱による温度上昇を金型の下部から上部に順次発現させる具体的手段は、図1の金型内にラクタム溶液を注入する速度を調整する。
すなわち、ラクタム溶液を金型に注入途中で金型下部では溶液の重合反応が始まり重合固化が進行し、この重合反応にともなって重合発熱が発生して金型1の下部にセットされている熱電対2が高温値を示す。
この熱電対の値を確認しながら下部、中部、上部と順次に重合による発熱温度が上昇するように、ラクタム溶液の金型内への注入速度を調整しながら重合成形を行う。
【0011】
図2は溶融ラクタムを金型に注入した際の金型内の各部位の温度上昇と時間の関係図であり、金型内に逐次注入された溶液が重合発熱して金型下部が先ず温度上昇し次いで中部及び上部と上昇し、ついに金型内の各部位の温度が一定の値となる。
【0012】
このように、金型の下部から上部へ向かって重合固化が進行し、内部残留気泡のないポリアミド樹脂成形体を得ることが出来た。また溶融ラクタムと比重を異にする充填材、補強材の添加材を添加した場合、添加材の沈降よりラクタム液の増粘が勝るため均一に分散することが可能となった。
【0013】
ここで、注入するラクタム溶液の配合や温度、金型の温度等を調整して重合速度を極端に速くすると金型の高さ方向で重合固化スピードに極端な差が生じ、重合成形された製品の表面に凹凸が発生し、外観不良を生じたり均一な物性のものが得られなくなる。また注入速度を極端に遅くした場合も重合成形された製品に同様な不良が生じる。
【0014】
【実施例】
以下、本発明を実施例および比較例により説明する。
実施例1
成形金型は図1に示す成形金型を160℃に保持したものを使用した。
ステンレス鋼製容器に、無水のεーカプロラクタム14kgを採り140〜160℃の温度に加熱し、これに重合助触媒のトリレンジイソシアネート33gとグラファイト2kgを添加混合した。……「A液」と呼ぶ
一方、別のステンレス鋼製容器に、無水のεーカプロラクタム1kgを採り、これに重合触媒の水素化ナトリウム(油性63%)9gを加え140〜160℃に調整した。……「B液」と呼ぶ
2台のポンプを用いて、 A液を5.65kg/min、B液を0.35kg/min、合計6kg/minの注入速度で成型型内に溶融ラクタム液を同時に注入した。注入と同時に金型各部位の混合溶液の重合発熱による温度上昇を熱電対2で測定したところ、下部から中部及び上部と順次発現していた。
約30分で金型から成形体を取り出し超音波探傷器で内部検査したが内部残留気泡は見られなかった。また外観も良好で、グラファイトの分散も成形体の各部位で良好であった。引張強度もASTM D638に準拠して測定したところ85MPa以上の強度を示し、各部位の差も5MPa以内であり良好であった。なお引張試験片は金型の高さ方向を試験片の長さ方向として採取した。
金型内に注入された溶融ラクタム液は、金型の下部から上部に固化が順次進行して重合成形された。
【0015】
比較例1
実施例1で、A液及びB液の注入速度比を同じにし、溶融ラクタム液の合計の注入速度を15kg/minに変更した以外は同様にして評価した。
金型各部位の混合溶液の重合発熱による温度上昇は上部から中部及び下部の順位に現れた。
成形体は内部残留気泡が見られ、外観は良好であるが、グラファイトの分散は不良、引張強度は良好であった。
また、金型に注入された溶融ラクタム液は、金型の上部から中部及び下部の順位に固化が進行した。
【0016】
【発明の効果】
本発明により、サイズ、形状を問わず、成形体に内部残留気泡が無く又外面にも凹凸の発生がなく、さらに充填材、補強材等の添加材を添加した際それらが均一に分散したポリアミド成形体を供給できる。
【図面の簡単な説明】
【図1】本発明に使用する成型金型の斜視図。
【図2】溶融ラクタムを金型に注入した際の金型内の各部位の温度上昇と時間との関係図。
【符号の説明】
1 金型
2 熱電対
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing a polyamide resin molded body having a predetermined shape such as a rod shape or a plate shape by anionic polymerization of lactam, and particularly when there are no internal residual bubbles and when additives such as a filler and a reinforcing material are added, The present invention relates to a method for producing a uniformly dispersed molded body.
[0002]
[Prior art]
In the method in which molten lactam heated to a predetermined temperature is injected into a preheated mold and anion polymerization is performed to form polyamide, a cavity defect called a bubble is generated inside the molded body depending on the size and shape of the molded body. Is a problem.
[0003]
This is due to a large volume shrinkage at the time of molding, and it takes a certain amount of time from the injection of the lactam solution into the mold until the start of polymerization, so the progress of polymerization varies at each site, or convection occurs after the lactam solution is injected. It is considered that one of the factors is that the upper solution temperature rises in the mold height direction and polymerizes from the upper part.
[0004]
In order to prevent the generation of such internal residual bubbles, a method for polymerizing a lactam solution under pressure has been proposed. In addition, when an additive such as a filler or a reinforcing material having a specific gravity different from that of the lactam solution is added, the particle size can be reduced for the problem that it is difficult to obtain a uniformly dispersed molded body that settles during polymerization. The method of increasing the viscosity of the lactam solution has been taken.
[0005]
[Problems to be solved by the invention]
The conventional method for eliminating the internal residual bubbles has been difficult to apply when the molding size is increased or a molded body having a different shape in the height direction is obtained. Furthermore, the equipment cost of the molding apparatus including a metal mold is high, which is a problem in terms of economy.
[0006]
In addition, when various additives are added to the lactam solution, the variation in the polymerization progress rate at each part becomes remarkable, the occurrence rate of internal residual bubbles increases in addition to poor dispersion, and it is difficult to suppress both by the conventional method. It is.
[0007]
[Means for Solving the Problems]
The present invention solves the above problems, and relates to a method for producing a polyamide resin molded body having no internal residual bubbles regardless of the size and shape of the molded body. In the presence of a cocatalyst, a method of producing a polyamide resin molding by injecting heat detection means into the molds provided in the lower, middle and upper parts of the mold, and maintaining the entire mold at a constant temperature The molten lactam was confirmed while detecting the temperature rise from the lower part of the mold to the middle part and the upper part by detecting the temperature rise due to the heat generated by polymerization of the molten lactam injected into the molded mold. The method for producing a polyamide resin molded body is characterized in that the injection speed of the resin is adjusted .
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described with reference to the drawings.
[0009]
FIG. 1 is a perspective view of a molding die used in the present invention, in which a thermocouple 2 is set at three locations of a lower portion, a middle portion, and an upper portion in a molding die 1 having a height of 600 mm, a width of 1200 mm, and a thickness of 20 mm. The entire mold was kept at 160 ° C.
[0010]
In the present invention, specific means for sequentially solidifying the polymer in the mold from the lower part to the upper part of the mold, or the temperature rise due to the polymerization heat of the polymer in the mold from the lower part to the upper part of the mold. As a specific means for sequentially developing, the rate at which the lactam solution is injected into the mold shown in FIG. 1 is adjusted.
That is, while the lactam solution is being injected into the mold, the polymerization reaction of the solution starts at the lower part of the mold and the solidification of the polymerization proceeds. The polymerization reaction generates heat and the thermoelectric set in the lower part of the mold 1. Pair 2 shows the high temperature value.
While confirming the value of this thermocouple, polymerization molding is performed while adjusting the injection rate of the lactam solution into the mold so that the exothermic temperature due to polymerization rises sequentially in the lower, middle and upper portions.
[0011]
FIG. 2 is a graph showing the relationship between the temperature rise of each part in the mold and the time when molten lactam is injected into the mold. It rises, then rises to the middle and upper part, and finally the temperature of each part in the mold becomes a constant value.
[0012]
Thus, polymerization solidification progressed from the lower part to the upper part of the mold, and a polyamide resin molded body having no internal residual bubbles could be obtained. In addition, when a filler having a specific gravity different from that of molten lactam or an additive for a reinforcing material is added, the thickening of the lactam solution is superior to the sedimentation of the additive, so that it can be uniformly dispersed.
[0013]
Here, if the polymerization rate is extremely increased by adjusting the composition and temperature of the lactam solution to be injected, the temperature of the mold, etc., there will be an extreme difference in the polymerization solidification speed in the mold height direction, and the polymer molded product As a result, irregularities appear on the surface of the film, resulting in poor appearance and no uniform physical properties. In addition, when the injection rate is extremely slow, similar defects occur in the polymer molded product.
[0014]
【Example】
Hereinafter, the present invention will be described with reference to examples and comparative examples.
Example 1
As the molding die, a molding die shown in FIG. 1 held at 160 ° C. was used.
In a stainless steel container, 14 kg of anhydrous ε-caprolactam was taken and heated to a temperature of 140 to 160 ° C., to which 33 g of tolylene diisocyanate as a polymerization promoter and 2 kg of graphite were added and mixed. ... Although it is called “Liquid A”, 1 kg of anhydrous ε-caprolactam was taken in another stainless steel container, and 9 g of sodium hydride (63% oily) as a polymerization catalyst was added to this to adjust to 140 to 160 ° C. . …… Using two pumps called “Liquid B”, liquid A is 5.65 kg / min, liquid B is 0.35 kg / min, and molten lactam liquid is poured into the mold at a total injection rate of 6 kg / min. Injected simultaneously. At the same time as the injection, the temperature rise due to the polymerization exotherm of the mixed solution at each part of the mold was measured with the thermocouple 2, and it was expressed sequentially from the lower part to the middle part and the upper part.
In about 30 minutes, the molded body was taken out from the mold and subjected to internal inspection with an ultrasonic flaw detector, but no internal residual bubbles were found. The appearance was also good, and the dispersion of graphite was good at each part of the compact. When the tensile strength was measured according to ASTM D638, it showed a strength of 85 MPa or more, and the difference in each part was within 5 MPa, which was good. In addition, the tensile test piece was extract | collected by making the height direction of a metal mold | die into the length direction of a test piece.
The melted lactam solution injected into the mold was polymerized as the solidification proceeded sequentially from the bottom to the top of the mold.
[0015]
Comparative Example 1
Evaluation was made in the same manner as in Example 1 except that the injection rate ratio of the solution A and the solution B was the same and the total injection rate of the molten lactam solution was changed to 15 kg / min.
The temperature rise due to the polymerization exotherm of the mixed solution in each part of the mold appeared from the top to the middle and the bottom.
The molded body had internal residual bubbles, and the appearance was good, but the dispersion of graphite was poor and the tensile strength was good.
Further, the molten lactam solution injected into the mold proceeded to solidify from the upper part of the mold to the middle part and the lower part.
[0016]
【The invention's effect】
By the present invention, regardless of size and shape, the molded body has no internal residual bubbles, and the outer surface is free of irregularities. Further, when an additive such as a filler or a reinforcing material is added, the polyamide is uniformly dispersed. A compact can be supplied.
[Brief description of the drawings]
FIG. 1 is a perspective view of a molding die used in the present invention.
FIG. 2 is a diagram showing the relationship between the temperature rise and time of each part in the mold when molten lactam is injected into the mold.
[Explanation of symbols]
1 Mold 2 Thermocouple

Claims (1)

溶融ラクタムをアニオン重合触媒及び助触媒の存在下で、熱検出手段を金型内部の下部、中部及び上部に設けた金型内に注入してポリアミド樹脂成形体を製造する方法であって、金型全体を一定温度に保持した金型内に注入された溶融ラクタムの重合発熱による温度上昇を前記熱検出手段で検出して金型の下部から中部及び上部に順次温度を上昇するように、温度上昇を確認しながら溶融ラクタムの注入速度を調整することを特徴とするポリアミド樹脂成形体の製造方法。The molten lactam in the presence of an anionic polymerization catalyst and a cocatalyst, the thermal detection means of the inner mold bottom, a method is injected into a mold provided in the middle and upper producing polyamide resin moldings, gold The temperature is increased so that the temperature rises from the lower part to the middle part and the upper part of the mold by detecting the temperature rise caused by the heat generated by polymerization of the molten lactam injected into the mold with the whole mold held at a constant temperature. A method for producing a polyamide resin molded article, wherein the injection rate of molten lactam is adjusted while confirming the rise .
JP19687898A 1998-07-13 1998-07-13 Manufacturing method of polyamide resin molded body Expired - Fee Related JP3734623B2 (en)

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JP3734623B2 true JP3734623B2 (en) 2006-01-11

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RU2640589C2 (en) * 2012-07-06 2018-01-10 Райн Хеми Райнау ГмбХ Catalysts for producing mould polyamide, method of their production and their application

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