JP2007160582A - Manufacturing method of foamed blow molded product - Google Patents

Manufacturing method of foamed blow molded product Download PDF

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JP2007160582A
JP2007160582A JP2005357170A JP2005357170A JP2007160582A JP 2007160582 A JP2007160582 A JP 2007160582A JP 2005357170 A JP2005357170 A JP 2005357170A JP 2005357170 A JP2005357170 A JP 2005357170A JP 2007160582 A JP2007160582 A JP 2007160582A
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thermoplastic synthetic
foamed
synthetic resin
thickener
manufacturing
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JP4786324B2 (en
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Teruo Shiraishi
輝男 白石
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Inoac Corp
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Inoue MTP KK
Inoac Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing method of a foamed blow molded product suitable for manufacturing an air conditioning foam duct made hard to collapse a foamed parison by blowing pressure, not lowering the foaming magnification of the molded product and made hard to cause perforation due to the breaking of foams in a thin-walled part. <P>SOLUTION: In the manufacturing method of the foamed blow molded product wherein a thermoplastic synthetic resin 21 and a foaming agent 23 are charged in an extruder 11 to extrude the foamed parison 27 and air is blown in the foamed parison 27 in a state that the foamed parison 27 is received in a mold 31 to perform blow molding, the foaming agent 23 is charged in the extruder 11 along with the thermoplastic synthetic resin 21 and a thickener 25 and kneaded with the thermoplastic synthetic resin 21 and the thickener 25 in the extruder 11 to extrude the foamed parison 27. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

この発明は、発泡中空成形品の製造方法に関し、特には発泡パリソンを用いてブロー成形によって発泡中空成形品を製造する方法に関する。   The present invention relates to a method for producing a foamed hollow molded article, and more particularly to a method for producing a foamed hollow molded article by blow molding using a foamed parison.

従来、熱可塑性合成樹脂と発泡剤を押出機に投入して発泡パリソンを押し出し、前記発泡パリソンを成形型に収納し発泡パリソンに気体を吹き込んでブロー成形を行うことにより、発泡中空成形品を製造することが行われている。   Conventionally, a foamed hollow molded product is manufactured by putting a thermoplastic synthetic resin and a foaming agent into an extruder, extruding the foamed parison, storing the foamed parison in a mold, and blowing the gas into the foamed parison. To be done.

しかし、従来の発泡中空成形品の製造方法によると、ブロー成形時の吹き込み圧で発泡パリソンの気泡が潰れて発泡倍率が低下したり、成形品の薄肉部で破泡を生じて穴があいたりする問題がある。さらに、発泡中空成形品により空調用発泡ダクトを構成する場合、発泡倍率の低下により減音性能が低くなる問題もある。   However, according to the conventional method for producing a hollow foam molded article, the foaming parison bubbles are crushed by the blowing pressure at the time of blow molding and the foaming ratio is reduced, or the thin part of the molded article causes bubble breakage and holes. There is a problem to do. Furthermore, when an air-conditioning foam duct is formed of a foamed hollow molded product, there is a problem that the sound reduction performance is lowered due to a decrease in foaming ratio.

特表2000−505752号公報JP 2000-505752 Gazette 特開2001−18283号公報JP 2001-18283 A

この発明は前記の点に鑑みなされたものであって、吹き込み圧で発泡パリソンの気泡が潰れにくく、また成形品の発泡倍率が低下せず、しかも薄肉部で破泡による穴あきを生じ難く、空調用発泡ダクトの製造に好適な発泡中空成形品の製造方法を提供する。   This invention has been made in view of the above points, and it is difficult for the foamed parison air bubbles to be crushed by the blowing pressure, the foaming ratio of the molded product does not decrease, and it is difficult to cause perforation due to foam breakage in the thin part, Provided is a method for producing a foamed hollow molded article suitable for producing a foam duct for air conditioning.

請求項1の発明は、熱可塑性合成樹脂と発泡剤を押出機に投入して発泡パリソンを押し出し、前記発泡パリソンを成形型に収納し前記発泡パリソンに気体を吹き込んでブロー成形を行う発泡中空成形品の製造方法において、前記熱可塑性合成樹脂及び増粘剤と共に前記発泡剤を前記押出機に投入し、前記押出機内で前記熱可塑性合成樹脂及び前記増粘剤に前記発泡剤を混練することを特徴とする。   The invention of claim 1 is a foam hollow molding in which a thermoplastic synthetic resin and a foaming agent are put into an extruder to extrude a foam parison, the foam parison is accommodated in a mold, and gas is blown into the foam parison to perform blow molding. In the manufacturing method of the product, the foaming agent is charged into the extruder together with the thermoplastic synthetic resin and the thickener, and the foaming agent is kneaded into the thermoplastic synthetic resin and the thickener in the extruder. Features.

請求項2の発明は、請求項1において、前記熱可塑性合成樹脂と前記増粘剤は、両者を混練した場合のメルトテンションが、190℃において105mN〜240mNであることを特徴とする。   The invention of claim 2 is characterized in that, in claim 1, the thermoplastic synthetic resin and the thickener have a melt tension of 105 mN to 240 mN at 190 ° C. when both are kneaded.

請求項3の発明は、請求項1または2において、前記熱可塑性合成樹脂が、熱可塑性合成樹脂100重量部中、HDPEを50〜90重量部、残りをLLDPEとすることを特徴とする。   A third aspect of the present invention is characterized in that, in the first or second aspect, the thermoplastic synthetic resin is 50 to 90 parts by weight of HDPE and the rest is LLDPE in 100 parts by weight of the thermoplastic synthetic resin.

請求項4の発明は、請求項1から3の何れか一項において、前記増粘剤が、前記熱可塑性合成樹脂100重量部に対して1〜5重量部であることを特徴とする。   The invention of claim 4 is characterized in that, in any one of claims 1 to 3, the thickener is 1 to 5 parts by weight with respect to 100 parts by weight of the thermoplastic synthetic resin.

本発明によれば、押出機内で熱可塑性合成樹脂と増粘剤に発泡剤を混練して発泡パリソンを押し出しているため、増粘剤の作用により、発泡パリソンを用いるブロー成形時に吹き込み圧で発泡パリソンの気泡が潰れにくく、また成形品の発泡倍率が低下せず、しかも薄肉部で破泡による穴あきを生じ難くなり、良好な発泡中空成形品を製造することができる。さらに、得られた発泡中空成形品が空調用発泡ダクトの場合、管壁の発泡倍率が高いことなどにより高い減音効果が得られる。   According to the present invention, since the foaming parison is extruded by kneading the foaming agent into the thermoplastic synthetic resin and the thickener in the extruder, the foaming is performed by blowing pressure at the time of blow molding using the foamed parison due to the action of the thickening agent. It is difficult for the air bubbles of the parison to be crushed, the foaming ratio of the molded product does not decrease, and it is difficult for the thin-walled portion to perforate due to foam breakage, and a good foamed hollow molded product can be produced. Furthermore, when the obtained foamed hollow molded article is a foam duct for air conditioning, a high sound reduction effect can be obtained due to the high foaming ratio of the tube wall.

また、熱可塑性合成樹脂と増粘剤は、両者を混練した場合のメルトテンションが、190℃において105mN〜240mNであることにより、ブロー成形時に発泡パリソンの気泡が一層破泡し難くなり、成形品の薄肉部で穴あきを生じ難くできる。   In addition, the thermoplastic synthetic resin and the thickener have a melt tension of 105 mN to 240 mN at 190 ° C. when both are kneaded, so that the foamed parison bubbles are more difficult to break during blow molding, and the molded product It is hard to produce a hole in the thin wall part.

さらに、熱可塑性合成樹脂100重量部中、HDPEを50〜90重量部、残りをLLDPEとすることにより、成形品の剛性低下を防ぐと共に、ブロー吹き込み圧によって気泡が潰れるのをより効果的に防ぐことができる。   Furthermore, 50 to 90 parts by weight of HDPE and LLDPE in 100 parts by weight of the thermoplastic synthetic resin and LLDPE prevent the deterioration of the rigidity of the molded product and more effectively prevent bubbles from being crushed by the blow-in pressure. be able to.

また、増粘剤を熱可塑性合成樹脂100重量部に対して1〜5重量部とすることにより、熱可塑性合成樹脂と増粘剤の混練後のメルトテンションを発泡中空成形品の製造に好適な範囲とすることができ、良好なブロー成形性を得ることができる。   Further, by setting the thickener to 1 to 5 parts by weight with respect to 100 parts by weight of the thermoplastic synthetic resin, the melt tension after kneading the thermoplastic synthetic resin and the thickener is suitable for producing a foamed hollow molded product. The range can be set, and good blow moldability can be obtained.

以下この発明の実施形態を詳細に説明する。図1は本発明の一実施例に用いられる製造装置の概略図である。   Hereinafter, embodiments of the present invention will be described in detail. FIG. 1 is a schematic view of a manufacturing apparatus used in one embodiment of the present invention.

本発明においては、押出機11に熱可塑性合成樹脂21と発泡剤23と増粘剤25を投入する。熱可塑性合成樹脂21と発泡剤23と増粘剤25は、予め混合することなく押出機11に投入してもよく、あるいは熱可塑性合成樹脂21と発泡剤23と増粘剤25のうち少なくとも二種類を予め混合しておいてもよい。また、熱可塑性合成樹脂21と増粘剤25を予め混練してペレット化し、前記ペレットと発泡剤を押出機11に投入してもよい。その場合、増粘剤が均一に分散し易くなって、品質の安定化効果が高くなる。   In the present invention, the thermoplastic synthetic resin 21, the foaming agent 23, and the thickener 25 are put into the extruder 11. The thermoplastic synthetic resin 21, the foaming agent 23, and the thickening agent 25 may be put into the extruder 11 without being mixed in advance, or at least two of the thermoplastic synthetic resin 21, the foaming agent 23, and the thickening agent 25 may be added. You may mix a kind beforehand. Alternatively, the thermoplastic synthetic resin 21 and the thickener 25 may be kneaded in advance and pelletized, and the pellet and the foaming agent may be charged into the extruder 11. In this case, the thickener is easily dispersed uniformly, and the quality stabilizing effect is enhanced.

前記押出機11内では、熱可塑性合成樹脂21と発泡剤23及び増粘剤25がスクリュー13によって混練されると共に加熱されて熱可塑性合成樹脂21が溶融し、また混練物のメルトテンション(溶融張力)が増粘剤25によって増大する。前記メルトテンションが増加した混練物を、前記混練物中に含まれる発泡剤23によって発泡させ、クロスヘッド15から発泡パリソン27にして押し出す。押し出された発泡パリソン27は前記熱可塑性合成樹脂21が溶融した状態となっている。そして押し出された発泡パリソン27を成形型31に収容し、前記成形型31を閉じて発泡パリソン27を密封し、前記クロスヘッド15の中心に設けられている気体吹き込みノズル(図示せず)から、前記成形型31内の発泡パリソン27にエアー等の気体を吹き込み、前記発泡パリソン27を膨張させて成形型31の内面33と接触させ、目的の発泡中空成形品形状に賦形する。前記膨張した発泡パリソンを冷却固化させて形状固定し、その後に成形型31を開いて発泡中空成形品を取り出す。なお、前記成形型31から取り出した発泡中空成形品に対して、その後必要に応じてバリ等の除去が行われる。   In the extruder 11, the thermoplastic synthetic resin 21, the foaming agent 23 and the thickener 25 are kneaded by the screw 13 and heated to melt the thermoplastic synthetic resin 21, and the melt tension (melting tension) of the kneaded product. ) Is increased by the thickener 25. The kneaded material having an increased melt tension is foamed by the foaming agent 23 contained in the kneaded material and extruded from the cross head 15 as a foamed parison 27. The extruded foamed parison 27 is in a state where the thermoplastic synthetic resin 21 is melted. Then, the extruded foam parison 27 is accommodated in a mold 31, the mold 31 is closed to seal the foam parison 27, and from a gas blowing nozzle (not shown) provided at the center of the crosshead 15, A gas such as air is blown into the foamed parison 27 in the mold 31 and the foamed parison 27 is expanded and brought into contact with the inner surface 33 of the mold 31 to form the desired foamed hollow molded product shape. The expanded foamed parison is cooled and solidified to fix the shape, and then the mold 31 is opened to take out the foamed hollow molded product. In addition, the burr | flash etc. are removed as needed with respect to the foaming hollow molded product taken out from the said shaping | molding die 31 after that.

なお、前記成形型31は、目的とする発泡中空成形品が、自動車用等の空調用発泡ダクトである場合、成形型の内面33がダクトの外面形状と等しくされる。   In addition, the said shaping | molding die 31 makes the inner surface 33 of a shaping | molding die equal to the outer surface shape of a duct, when the foaming hollow molded product made into the objective is a foaming duct for air conditioning, such as a motor vehicle.

前記熱可塑性合成樹脂21は、ブロー成形可能なものであれば特に限定されず、目的とする発泡中空成形品に求められる物性に応じて決定される。使用可能な熱可塑性合成樹脂として、例えばポリエチレン、ポリプロピレン、ポリ塩化ビニル樹脂、ポリスチレン、ポリエチレンテレフタレート(PET)等を挙げることができる。特に、熱可塑性合成樹脂21は、熱可塑性合成樹脂100重量部中50〜90重量部をHDPE(高密度ポリエチレン)、残りをLLDPE(直鎖状低密度ポリエチレン)とするのが好ましい。HDPEが50重量部未満の場合(LLDPEが50重量部を超える場合)、成形品としての剛性が低下するようになり、一方HDPEが90重量部を超える場合(LLDPEが10重量部未満の場合)、ブロー成形時の吹き込み圧によって発泡パリソンの気泡が潰れて発泡倍率が低下するようになる。   The thermoplastic synthetic resin 21 is not particularly limited as long as it can be blow-molded, and is determined according to the physical properties required for the intended foamed hollow molded article. Examples of the thermoplastic synthetic resin that can be used include polyethylene, polypropylene, polyvinyl chloride resin, polystyrene, and polyethylene terephthalate (PET). In particular, the thermoplastic synthetic resin 21 is preferably 50 to 90 parts by weight of HDPE (high density polyethylene) and 100 parts by weight of thermoplastic synthetic resin 21 with LLDPE (linear low density polyethylene). When the HDPE is less than 50 parts by weight (when the LLDPE exceeds 50 parts by weight), the rigidity of the molded product decreases, while when the HDPE exceeds 90 parts by weight (when the LLDPE is less than 10 parts by weight) The foaming parison bubbles are crushed by the blowing pressure at the time of blow molding, and the foaming ratio is lowered.

前記発泡剤23は、公知の発泡中空成形品の製造方法に使用される化学発泡剤や物理発泡剤を制限なく使用することができる。また、前記発泡剤23は、図ではペレット状で示されているが、ペレット状に限られるものではない。化学発泡剤(分解型発泡剤)としては、炭酸水素ナトリウム、クエン酸ナトリウム、アゾジカルボンアミド、ジニトロソペンタメチレンテトラミン等を挙げることができる。また、物理発泡剤(揮発性発泡剤)としてはプロパン、ノルマルブタン、イソブタン、ノルマルペンタン、イソペンタン、ノルマルヘキサン、イソヘキサン、塩化メチル、炭酸ガス、窒素ガス等を挙げることができる。なお、化学発泡剤と物理発泡剤を併用してもよい。   As the foaming agent 23, a chemical foaming agent or a physical foaming agent used in a known method for producing a hollow foam molded article can be used without limitation. Moreover, although the said foaming agent 23 is shown by the pellet form in the figure, it is not restricted to a pellet form. Examples of the chemical foaming agent (decomposable foaming agent) include sodium hydrogen carbonate, sodium citrate, azodicarbonamide, dinitrosopentamethylenetetramine and the like. Examples of physical foaming agents (volatile foaming agents) include propane, normal butane, isobutane, normal pentane, isopentane, normal hexane, isohexane, methyl chloride, carbon dioxide gas, nitrogen gas, and the like. A chemical foaming agent and a physical foaming agent may be used in combination.

前記増粘剤25は、前記押出機における混練物のメルトテンションを増加させるものであれば使用することができる。具体的には、増粘剤25として、ポリテトラフルオロエチレン(PTFE)のアクリル変性品を挙げることができる。前記増粘剤25の添加量は、前記熱可塑性合成樹脂21の100重量部に対して1〜5重量部が好ましい。1重量部を下回ると、熱可塑性合成樹脂と増粘剤の混練後のメルトテンションが、発泡中空成形品の製造に好適な範囲の下限、本実施例では190℃で105mNより低くなって、ブロー成形時に発泡パリソンの気泡が一層破泡し易くなり、成形品の薄肉部で穴あきを生じ易くなる。それに対して増粘剤が5重量部を超えると、熱可塑性合成樹脂と増粘剤の混練後のメルトテンションが、発泡中空成形品の製造に好適な範囲の上限、本実施例では190℃で240mNより高くなって、パリソン自体のスウェルが大きくなりブロー成形の生産性が低下する。   The thickener 25 can be used as long as it increases the melt tension of the kneaded material in the extruder. Specifically, examples of the thickener 25 include an acrylic modified product of polytetrafluoroethylene (PTFE). The addition amount of the thickener 25 is preferably 1 to 5 parts by weight with respect to 100 parts by weight of the thermoplastic synthetic resin 21. If the amount is less than 1 part by weight, the melt tension after kneading the thermoplastic synthetic resin and the thickener is lower than the lower limit of the range suitable for the production of the foamed hollow molded product, in this example, lower than 105 mN at 190 ° C. During molding, the foamed parison bubbles are more likely to break, and holes are easily formed in the thin portion of the molded product. On the other hand, if the thickener exceeds 5 parts by weight, the melt tension after kneading the thermoplastic synthetic resin and the thickener is the upper limit of the range suitable for the production of the foamed hollow molded article, in this example 190 ° C. When it becomes higher than 240 mN, the swell of the parison itself becomes large and the productivity of blow molding decreases.

なお、本発明におけるメルトテンションの測定は、図2に示す装置により測定した。すなわち、底部にφ2.0mm×L20mmの孔42が形成された内径9.5mmの筒状体41を垂直に配置し、前記筒状体41内に熱可塑性合成樹脂と増粘剤の混合物Pを投入して190℃に保ち、前記筒状体41内の混合物Pを押圧板43により20mm/minの速度で押圧して前記筒状体41の底部の孔42から下方へ押し出すと共に、押し出した混合物P1をリール44,45により水平方向へ向きを変えて3.1m/minの速度で引っ張り、また、前記水平方向へ向きを変えるリール44については張力測定機46と接続し、張力測定機46の値でメルトテンションを測定した。   In addition, the measurement of the melt tension in this invention was measured with the apparatus shown in FIG. That is, a cylindrical body 41 having an inner diameter of 9.5 mm in which a hole 42 of φ2.0 mm × L20 mm is formed at the bottom is arranged vertically, and a mixture P of a thermoplastic synthetic resin and a thickener is placed in the cylindrical body 41. The mixture P is charged and maintained at 190 ° C., and the mixture P in the cylindrical body 41 is pressed by the pressing plate 43 at a speed of 20 mm / min to be pushed downward from the hole 42 at the bottom of the cylindrical body 41 and the extruded mixture. P1 is rotated in the horizontal direction by reels 44 and 45 and pulled at a speed of 3.1 m / min. The reel 44 that changes the direction in the horizontal direction is connected to a tension measuring device 46. The melt tension was measured by value.

熱可塑性合成樹脂としてHDPE(品名:KB148A、日本ポリエチレン株式会社製)とLLDPE(品名:ノバテック(登録商標)UF840、日本ポリエチレン株式会社製)を用い、また増粘剤としてポリテトラフルオロエチレン(PTFE)のアクリル変性品(品名:メタブレンA−3000、三菱レイヨン株式会社製)を用い、前記HDPEとLLDPE及び増粘剤を表1のNo.1〜14の重量部割合にして混練材を作成し、その混練材について図2の方法でメルトテンションを測定した。また、発泡剤として化学発泡剤(品名:EE405D、永和化成工業株式会社製)を用い、前記HDPE、LLDPE、増粘剤及び発泡剤を表1のNo.1〜13の重量部割合にして押出機に投入し、発泡パリソンを形成した後、ダクト用成形型を用いて図3に示す自動車の空調用発泡ダクトをブロー成形した。   HDPE (product name: KB148A, manufactured by Nippon Polyethylene Co., Ltd.) and LLDPE (product name: Novatec (registered trademark) UF840, manufactured by Nippon Polyethylene Co., Ltd.) are used as thermoplastic synthetic resins, and polytetrafluoroethylene (PTFE) is used as a thickener. Acrylic modified product (product name: Metabrene A-3000, manufactured by Mitsubishi Rayon Co., Ltd.) was used. A kneaded material was prepared at a weight part ratio of 1 to 14, and the melt tension of the kneaded material was measured by the method shown in FIG. Further, a chemical foaming agent (product name: EE405D, manufactured by Eiwa Kasei Kogyo Co., Ltd.) was used as the foaming agent, and the HDPE, LLDPE, thickener and foaming agent were designated No. 3 to 13 parts by weight were charged into an extruder to form a foamed parison, and then a foamed duct for automobile air conditioning shown in FIG. 3 was blow molded using a duct molding die.

Figure 2007160582
Figure 2007160582

このようにして得られた空調用発泡ダクトについて、ダクト剛性、発泡状態、穴の有無、成形性を判断し、総合判定を行った。判定結果は表1に示すとおりである。なお、ダクト剛性はダクトとして十分の剛性が有るか否かにより判断し、十分満足のできるものを「○」、少し劣るが満足できるものを「△」、不満足のものを「×」とした。また、発泡状態は成形品を切断して切断面の気泡が発泡しているか否かで判断し、十分発泡しているものを「○」、気泡状態が少し残っているものを「△」、気泡が潰れてしまっているものを「×」とした。一方、穴の有無は図3に示した空調用発泡ダクトにおいて薄肉となるコーナー部51でピンホールが発生しているか否かを黙視で観察し、ピンホールが無いものを「○」、わずかに有るものを「△」、多く有るものを「×」とした。   The air-conditioning foamed duct thus obtained was subjected to a comprehensive judgment by judging duct rigidity, foamed state, presence of holes, and moldability. The determination results are as shown in Table 1. The duct rigidity was determined based on whether or not the duct had sufficient rigidity, and “○” was given to the satisfactory one, “△” was given to the one that was slightly inferior, and “X” was shown to be unsatisfactory. In addition, the foamed state is determined by cutting the molded product to determine whether or not the bubbles on the cut surface are foamed. The case where the bubbles were crushed was designated as “x”. On the other hand, the presence or absence of a hole is determined by observing whether or not a pinhole is generated in the thin corner portion 51 in the air-conditioning foamed duct shown in FIG. “△” indicates that there are many, and “×” indicates that there are many.

表1のNo.3〜8の結果から、増粘剤を用いることによって発泡状態及び穴あきを改善できることがわかる。さらに、No.1,2の結果から熱可塑性合成樹脂(HDPEとLLDPE)と増粘剤の混練後のメルトテンションが低いと発泡状態及び穴あきにおいて不利になることが理解できる。一方、No.9及び12のように、熱可塑性合成樹脂(HDPEとLLDPE)と増粘剤の混練後のメルトテンションが、190℃において240mNを超えると、パリソンのスウェルが大になってブロー生産性が低下するようになる。さらに、No.2,5,8,11,13,14の結果から、熱可塑性合成樹脂100重量部中、HDPEが50重量部〜90重量部、残りがLLDPEであるとダクト剛性や発泡状態を改善できることがわかる。また、No.3〜12の結果から、増粘剤の量は1〜5重量部が好ましいことがわかる。   No. in Table 1 From the results of 3 to 8, it can be seen that the foaming state and perforation can be improved by using a thickener. Furthermore, no. From the results of 1 and 2, it can be understood that if the melt tension after kneading the thermoplastic synthetic resin (HDPE and LLDPE) and the thickener is low, it is disadvantageous in the foamed state and perforation. On the other hand, no. As in 9 and 12, when the melt tension after kneading the thermoplastic synthetic resin (HDPE and LLDPE) and the thickener exceeds 240 mN at 190 ° C., the swell of the parison becomes large and the blow productivity decreases. It becomes like this. Furthermore, no. From the results of 2, 5, 8, 11, 13, and 14, it is understood that duct rigidity and foaming state can be improved when HDPE is 50 to 90 parts by weight and the rest is LLDPE in 100 parts by weight of thermoplastic synthetic resin. . No. From the results of 3 to 12, it is understood that the amount of the thickener is preferably 1 to 5 parts by weight.

本発明の一実施例に用いる製造装置の概略図である。It is the schematic of the manufacturing apparatus used for one Example of this invention. 本発発明におけるメルトテンションの測定方法を示す図である。It is a figure which shows the measuring method of the melt tension in this invention. 本発明の製造方法で得られた自動車の空調用発泡ダクトの一実施形態を示す斜視図である。It is a perspective view which shows one Embodiment of the foaming duct for an air conditioning of the motor vehicle obtained with the manufacturing method of this invention.

符号の説明Explanation of symbols

11 押出機
13 スクリュー
15 クロスヘッド
21 熱可塑性合成樹脂
23 発泡剤
25 増粘剤
27 発泡パリソン
31 成形型
DESCRIPTION OF SYMBOLS 11 Extruder 13 Screw 15 Crosshead 21 Thermoplastic synthetic resin 23 Foaming agent 25 Thickener 27 Foam parison 31 Mold

Claims (4)

熱可塑性合成樹脂と発泡剤を押出機に投入して発泡パリソンを押し出し、前記発泡パリソンを成形型に収納し前記発泡パリソンに気体を吹き込んでブロー成形を行う発泡中空成形品の製造方法において、
前記熱可塑性合成樹脂及び増粘剤と共に前記発泡剤を前記押出機に投入し、前記押出機内で前記熱可塑性合成樹脂及び前記増粘剤に前記発泡剤を混練することを特徴とする発泡中空成形品の製造方法。
In the manufacturing method of a foamed hollow molded article in which a thermoplastic synthetic resin and a foaming agent are put into an extruder to extrude a foamed parison, the foamed parison is accommodated in a mold, and gas is blown into the foamed parison to perform blow molding.
The foamed hollow molding characterized in that the foaming agent is charged into the extruder together with the thermoplastic synthetic resin and the thickener, and the foaming agent is kneaded into the thermoplastic synthetic resin and the thickener in the extruder. Product manufacturing method.
前記熱可塑性合成樹脂と前記増粘剤は、両者を混練した場合のメルトテンションが、190℃において105mN〜240mNであることを特徴とする請求項1に記載の発泡中空成形品の製造方法。   2. The method for producing a hollow foam molded article according to claim 1, wherein the thermoplastic synthetic resin and the thickener have a melt tension of 105 mN to 240 mN at 190 ° C. when both are kneaded. 前記熱可塑性合成樹脂は、熱可塑性合成樹脂100重量部中、HDPEが50〜90重量部、残りがLLDPEであることを特徴とする請求項1または2に記載の発泡中空成形品の製造方法。   The said thermoplastic synthetic resin is 50-90 weight part of HDPE in 100 weight part of thermoplastic synthetic resins, and the remainder is LLDPE, The manufacturing method of the foaming hollow molded product of Claim 1 or 2 characterized by the above-mentioned. 前記増粘剤は、前記熱可塑性合成樹脂100重量部に対して1〜5重量部であることを特徴とする請求項1から3の何れか一項に記載の発泡中空成形品の製造方法。
The said thickener is 1-5 weight part with respect to 100 weight part of said thermoplastic synthetic resins, The manufacturing method of the foaming hollow molded article as described in any one of Claim 1 to 3 characterized by the above-mentioned.
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KR101516404B1 (en) 2012-08-22 2015-05-04 영보화학 주식회사 Manufacturing method of an Air duct for air conditioning system of automobile
EP3617258A4 (en) * 2017-04-27 2020-03-25 Kyoraku Co., Ltd. Foam duct

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CN110893674A (en) * 2019-11-26 2020-03-20 南通恒趣新材料有限公司 Full-automatic blow molding process

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JPH11124478A (en) * 1997-08-22 1999-05-11 Mitsubishi Rayon Co Ltd Improver for melt tension for polyolefin resin and its production
JP2000159947A (en) * 1998-11-25 2000-06-13 Tosoh Corp Resin composition
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JPH0524126A (en) * 1991-07-19 1993-02-02 Sekisui Chem Co Ltd Manufacture of polyolefin resin crosslinked foam
JPH11124478A (en) * 1997-08-22 1999-05-11 Mitsubishi Rayon Co Ltd Improver for melt tension for polyolefin resin and its production
JP2000159947A (en) * 1998-11-25 2000-06-13 Tosoh Corp Resin composition
JP2002192601A (en) * 2000-12-25 2002-07-10 Jsp Corp Manufacturing method of expanded form having olefin resin foamed layer

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101516404B1 (en) 2012-08-22 2015-05-04 영보화학 주식회사 Manufacturing method of an Air duct for air conditioning system of automobile
EP3617258A4 (en) * 2017-04-27 2020-03-25 Kyoraku Co., Ltd. Foam duct
US11242439B2 (en) 2017-04-27 2022-02-08 Kyoraku Co., Ltd. Foam duct

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