JP5350302B2 - Mannequin manufacturing method - Google Patents

Mannequin manufacturing method Download PDF

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JP5350302B2
JP5350302B2 JP2010069497A JP2010069497A JP5350302B2 JP 5350302 B2 JP5350302 B2 JP 5350302B2 JP 2010069497 A JP2010069497 A JP 2010069497A JP 2010069497 A JP2010069497 A JP 2010069497A JP 5350302 B2 JP5350302 B2 JP 5350302B2
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mannequin
mold
resin
manufacturing
biomass
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JP2011200366A (en
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勲 岡田
秀明 上杉
隆太郎 玉田
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株式会社ヤマトマネキン
株式会社玉田製作所
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C49/00Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
    • B29C49/02Combined blow-moulding and manufacture of the preform or the parison
    • B29C49/04Extrusion blow-moulding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00Other particular articles
    • B29L2031/702Imitation articles, e.g. statues, mannequins

Description

本発明は、ブロー成形によりマネキンを製造するマネキンの製造方法に関する。   The present invention relates to a mannequin manufacturing method for manufacturing a mannequin by blow molding.

従来、マネキンの製造方法は、ポリエチレン樹脂をホッパーに入れ、ホッパーからポリエチレン樹脂をスクリュー内蔵管内に供給する。スクリュー内蔵管内でポリエチレン樹脂を融解・攪拌して射出室へ送る。射出室内のポリエチレン樹脂は、ダイスの隙間から金型内へ射出されて熔融中空体を形成する。金型を閉じてから、ノズルにより熔融中空体内に圧縮空気を送ると、熔融中空体が膨脹して金型内面に接触する。この状態で冷却させるとポリエチレン樹脂が硬化してマネキンが成形され、金型を分割してこのマネキンを取り出し、バリをとって完成する。   Conventionally, the manufacturing method of a mannequin puts a polyethylene resin into a hopper, and supplies the polyethylene resin from the hopper into a screw built-in pipe. The polyethylene resin is melted and agitated in the screw built-in tube and sent to the injection chamber. The polyethylene resin in the injection chamber is injected from the gap between the dies into the mold to form a molten hollow body. When the mold is closed and compressed air is sent into the molten hollow body by the nozzle, the molten hollow body expands and contacts the inner surface of the mold. When cooled in this state, the polyethylene resin is cured and a mannequin is formed, the mold is divided, the mannequin is taken out, and the burr is removed to complete.

従来の製造方法によって製造されたマネキンは、石油由来の熱可塑性樹脂によって成形されているので、産業廃棄物として処理され、簡単に廃棄できるものではなく、しかも廃棄の際に発生する二酸化炭素などの地球温暖化ガスが大量に増加するので、自然環境にあまり好ましいものではない。本願出願人は、このような観点から、産業廃棄物ではなく一般廃棄物として廃棄処理でき、しかも廃棄にあたって二酸化炭素の増加が少なく自然環境に優しい、バイオマス樹脂からなるマネキン人形の製造方法を提案した(特許文献1)。   Mannequins manufactured by conventional manufacturing methods are molded from petroleum-derived thermoplastics, so they are treated as industrial waste and cannot be easily disposed of, and carbon dioxide generated during disposal Since global warming gas increases in large quantities, it is not very favorable for the natural environment. From this point of view, the applicant of the present application has proposed a method for manufacturing a mannequin doll made of biomass resin that can be disposed of as general waste instead of industrial waste, and that is free from carbon dioxide during disposal and is friendly to the natural environment. (Patent Document 1).

上記した本願出願人が提案したマネキン人形の製造方法は、ベース素材前型及び後型の内面にバイオマス熱硬化性樹脂溶液を塗り重ね、次にバイオマスシートを貼り、さらにこのバイオマスシートにバイオマス熱硬化性樹脂溶液を塗って前半身及び後半身を形成し、前型と後型を重ね合わせて前半身と後半身を接合させ、硬化後に前型及び後型を外すと、マネキン人形が形成される。   The manufacturing method of the mannequin doll proposed by the applicant of the present application described above is to apply a biomass thermosetting resin solution to the inner surfaces of the base material front mold and the rear mold, and then paste a biomass sheet, and further biomass thermosetting to this biomass sheet. A mannequin doll is formed when the front and back molds are overlapped by applying the functional resin solution, the front mold and the back mold are overlapped, and the front and back molds are removed after curing. .

特願2009−92609号Japanese Patent Application No. 2009-92609

上記した本願出願人が提案した製造方法により製造したマネキン人形は、一般廃棄物として廃棄処理でき、廃棄処理に発生する有害物質、二酸化炭素の発生が少なく、そのため、自然環境に優しいものである。しかし、このマネキン人形の製造方法は、手作業で行うため製作が面倒であり、しかも均一に塗り重ねる技術及び所定の厚みに塗り重ねる技術等の熟練性が必要であり、誰でもが簡単に製造することができないという問題点があった。   The mannequin doll manufactured by the above-described manufacturing method proposed by the applicant of the present application can be disposed of as general waste, generates little harmful substances and carbon dioxide generated in the disposal, and is therefore friendly to the natural environment. However, this mannequin doll manufacturing method is cumbersome because it is performed manually, and it requires skill such as uniform coating technology and coating technology to a predetermined thickness. There was a problem that could not be done.

本願発明は、上記問題点に鑑み案出したものであって、誰でも簡単にバイオマス樹脂からなるマネキンを製造することができるマネキンの製造方法を提供することを目的とする。   The present invention has been devised in view of the above problems, and an object of the present invention is to provide a mannequin manufacturing method by which anyone can easily manufacture a mannequin made of biomass resin.

本願請求項記載のマネキンの製造方法は、上記目的を達成するため、ブロー成形によって製造するマネキンの製造方法であって、5〜85重量%の貝殻材料と15〜95重量%のポリエチレン樹脂からなるバイオマス樹脂のペレットをホッパーからスクリュー内蔵管に送り、スクリュー内蔵管内において前記バイオマス樹脂のペレットを加熱融解し、この融解したバイオマス樹脂をスクリューにて攪拌しつつ射出室内へ移送し、射出室内においてバイオマス樹脂を貝殻材料の適正融解温度である180℃〜190℃まで加熱した後にマネキン金型内に射出して熔融中空体を形成し、当該熔融中空体に圧縮空気を吹き込み、熔融中空体を膨張させてマネキン金型の内面に接触させ、熔融中空体をマネキン金型の内面に接触させた状態で冷却固化させてマネキンを製造することを特徴とする。
Mannequins manufacturing method of the present claim 1 wherein, in order to achieve the above object, a mannequin manufacturing method for manufacturing by blow molding, from 5 to 85 wt% shells material and 15-95 wt% of a polyethylene resin The biomass resin pellets are sent from the hopper to the screw built-in tube, the biomass resin pellets are heated and melted in the screw built-in tube, and the melted biomass resin is transferred to the injection chamber while stirring with the screw. After the resin is heated to 180 ° C to 190 ° C, which is the appropriate melting temperature for the shell material, it is injected into a mannequin mold to form a molten hollow body, and compressed air is blown into the molten hollow body to expand the molten hollow body. With the inner surface of the mannequin mold and the molten hollow body in contact with the inner surface of the mannequin mold. It is characterized by manufacturing a mannequin.

本願発明に係るマネキンの製造方法によれば、ブロー成形により、誰でも簡単にバイオマス樹脂からなるマネキンを製造することができるという効果がある。本願発明に係るマネキンの製造方法により製造されたマネキンは、一般廃棄物として廃棄処理でき、廃棄処理に発生する有害物質、二酸化炭素の発生が少なく、そのため、自然環境に優しいという効果がある。   According to the manufacturing method of the mannequin which concerns on this invention, there exists an effect that anyone can manufacture the mannequin which consists of biomass resin easily by blow molding. The mannequin manufactured by the method for manufacturing a mannequin according to the present invention can be disposed of as general waste, and generates less harmful substances and carbon dioxide generated in the disposal, and thus has an effect of being friendly to the natural environment.

本願発明に係るマネキンの製造方法の第1工程を示す断面図である。It is sectional drawing which shows the 1st process of the manufacturing method of the mannequin which concerns on this invention. 本願発明に係るマネキンの製造方法の第2工程を示す断面図である。It is sectional drawing which shows the 2nd process of the manufacturing method of the mannequin which concerns on this invention. 本願発明に係るマネキンの製造方法の第3工程を示す断面図である。It is sectional drawing which shows the 3rd process of the manufacturing method of the mannequin which concerns on this invention.

マネキンMをブロー成形によって製造するための製造装置について説明する。図1に示すように、製造装置1は、樹脂材料を蓄積するホッパー2と、樹脂材料を融解しながら射出室11に送るスクリュー内蔵管6と、マネキンMを成形するための金型16と、金型16内に圧縮空気を送り込むノズル23とからなる。ホッパー2は、口部3開口に向かって傾斜する傾斜面5を有し、口部3がスクリュー内蔵管6に接続され、内部の樹脂材料を自重によりスクリュー内蔵管6内に送るようになっている。   A manufacturing apparatus for manufacturing the mannequin M by blow molding will be described. As shown in FIG. 1, the manufacturing apparatus 1 includes a hopper 2 that accumulates a resin material, a screw built-in pipe 6 that is sent to the injection chamber 11 while melting the resin material, a mold 16 for molding the mannequin M, It consists of a nozzle 23 that feeds compressed air into the mold 16. The hopper 2 has an inclined surface 5 that is inclined toward the opening of the mouth portion 3, the mouth portion 3 is connected to the screw built-in tube 6, and the internal resin material is fed into the screw built-in tube 6 by its own weight. Yes.

スクリュー内蔵管6には、スクリュー7が設けられている。スクリュー7は、駆動モータ9とプーリ等の動力伝達手段10によって一方向に回転するように構成されている。また、スクリュー内蔵管6は、図示しない手段によって加熱され、内部の樹脂材料を加熱融解させるようになっている。スクリュー内蔵管6の先端は、射出室11の側面に接続され、スクリュー内蔵管6内で融解された樹脂材料がスクリュー7によって攪拌されて射出室11内に移送される。   The screw built-in pipe 6 is provided with a screw 7. The screw 7 is configured to rotate in one direction by a drive motor 9 and power transmission means 10 such as a pulley. The screw built-in tube 6 is heated by means (not shown) to heat and melt the internal resin material. The tip of the screw built-in tube 6 is connected to the side surface of the injection chamber 11, and the resin material melted in the screw built-in tube 6 is stirred by the screw 7 and transferred into the injection chamber 11.

射出室11は、下部が開放されており、下部に円板状のダイス12が設けられている。射出室11内でも樹脂材料がさらに加熱され、樹脂材料はダイス12と射出室11の隙間13から金型16内に円筒状に射出されて熔融中空体17を形成する。なお、射出室11内にピストンを設け、当該ピストンにより樹脂材料を射出するようにしても良い。金型16は、前半体19と後半体20とからなり、図2に示すように、前半体19と後半体20とが接合して内部にマネキンの雌型21が形成される。金型16は、前半体19と後半体20が離間している状態の時に、前記射出室11から射出された樹脂材料の熔融中空体17が前半体19と後半体20間で形成される。金型16の下部には、金型16内に圧縮空気を送り込むノズル23の先端を金型16内部に突出させる挿通孔25が形成されている。   The lower part of the injection chamber 11 is open, and a disk-shaped die 12 is provided at the lower part. The resin material is further heated in the injection chamber 11, and the resin material is injected into the mold 16 in a cylindrical shape from the gap 13 between the die 12 and the injection chamber 11 to form a molten hollow body 17. A piston may be provided in the injection chamber 11 and the resin material may be injected by the piston. The mold 16 includes an anterior half body 19 and a posterior half body 20, and as shown in FIG. 2, the anterior half body 19 and the posterior half body 20 are joined to form a mannequin female die 21 therein. In the mold 16, when the front half body 19 and the rear half body 20 are separated from each other, a molten hollow body 17 of the resin material injected from the injection chamber 11 is formed between the front half body 19 and the rear half body 20. An insertion hole 25 is formed in the lower part of the mold 16 so that the tip of a nozzle 23 that feeds compressed air into the mold 16 protrudes into the mold 16.

図1に示すように、製造装置1は、ホッパー2内に樹脂材料をいれて蓄積すると、ホッパー2内の樹脂材料がスクリュー内蔵管6に送られる。スクリュー内蔵管6内に送られた樹脂材料は、加熱溶融されて流体状になり、駆動モータ9により回転させられているスクリュー7により攪拌されて射出室11内に送られる。射出室11内に送られた樹脂材料は、さらに加熱されて、ダイス12と射出室11の隙間13から金型16内に円筒状に射出されて熔融中空体17を形成する。この時、金型16は、前半体19と後半体20と分離されている。図2に示すように、前半体19と後半体20とを接合して内部にマネキンの雌型21を形成し、ノズル23により熔融中空体17に圧縮空気を送り込むと、熔融中空体17が膨脹してマネキンの雌型21に圧接する。金型16を冷却すると、樹脂材料が硬化してマネキンMが成形される。図3に示すように、金型16内のマネキンMは、金型16を前半体19と後半体20に分離することによって取り出すことができる。   As shown in FIG. 1, when the manufacturing apparatus 1 puts and accumulates a resin material in the hopper 2, the resin material in the hopper 2 is sent to the screw built-in pipe 6. The resin material sent into the screw built-in pipe 6 is heated and melted to become a fluid, and is stirred by the screw 7 rotated by the drive motor 9 and sent into the injection chamber 11. The resin material sent into the injection chamber 11 is further heated and injected into the mold 16 through the gap 13 between the die 12 and the injection chamber 11 into a cylindrical shape to form a molten hollow body 17. At this time, the mold 16 is separated from the front half 19 and the rear half 20. As shown in FIG. 2, when the front half body 19 and the rear half body 20 are joined to form a mannequin female die 21 and compressed air is fed into the molten hollow body 17 by the nozzle 23, the molten hollow body 17 expands. Then, it is pressed against the mannequin female die 21. When the mold 16 is cooled, the resin material is cured and the mannequin M is molded. As shown in FIG. 3, the mannequin M in the mold 16 can be taken out by separating the mold 16 into a front half 19 and a rear half 20.

上記したようにマネキンをブロー成形によって製造する場合の樹脂材料は、5〜95重量%のバイオマス材料と5〜95重量%の熱可塑性樹脂からなるバイオマス樹脂であって、粒状化したペレットである。当該ペレットをホッパー2からスクリュー内蔵管6に送り、スクリュー内蔵管6内において前記バイオマス樹脂のペレットを加熱融解し、このバイオマス樹脂をスクリュー7にて攪拌しつつ射出室11内へ移送する。射出室11内においてバイオマス樹脂をバイオマス材料の適正融解温度まで加熱した後にマネキン金型16内に射出して熔融中空体17を形成する。次に、当該熔融中空体17に圧縮空気を吹き込み、熔融中空体17を膨張させてマネキン金型16の内面に接触させ、熔融中空体17をマネキン金型16の内面に接触させた状態で冷却固化させてマネキンMを製造する。   As described above, the resin material in the case where the mannequin is manufactured by blow molding is a biomass resin composed of 5 to 95% by weight of a biomass material and 5 to 95% by weight of a thermoplastic resin, and is a granulated pellet. The pellets are sent from the hopper 2 to the screw built-in pipe 6, the biomass resin pellets are heated and melted in the screw built-in pipe 6, and the biomass resin is transferred into the injection chamber 11 while being stirred by the screw 7. In the injection chamber 11, the biomass resin is heated to an appropriate melting temperature of the biomass material, and then injected into the mannequin mold 16 to form the molten hollow body 17. Next, compressed air is blown into the molten hollow body 17, the molten hollow body 17 is expanded and brought into contact with the inner surface of the mannequin mold 16, and the molten hollow body 17 is cooled while being in contact with the inner surface of the mannequin mold 16. Mannequin M is produced by solidification.

適正融解温度とは、熱可塑性樹脂をブロー成形する時の最適な融解温度であって、高すぎると粘性が低くなってドローダウンが大きくなり、低すぎると粘性が高くなって成形不良を起こし易くなる。素材によって適正融解温度が異なり、ポリエチレン樹脂では、170℃〜180℃、バイオマス材料のお米材では、165℃〜170℃、同じくバイオマス材料の貝殻材では、180℃〜190℃が適正融解温度である。また、バイオマス樹脂の重量比は、廃棄処理に伴う二酸化炭素の発生の増加の観点及び一般家庭ゴミとして廃棄処理できる等の観点から、バイオマス材料が51重量%以上、熱可塑性樹脂が49重量%以下であることが望ましい。   The proper melting temperature is the optimum melting temperature when blow molding a thermoplastic resin. If it is too high, the viscosity will be low and drawdown will be large, and if it is too low, the viscosity will be high and prone to molding defects. Become. The proper melting temperature varies depending on the material. The appropriate melting temperature is 170 ° C to 180 ° C for polyethylene resin, 165 ° C to 170 ° C for rice of biomass material, and 180 ° C to 190 ° C for shell material of biomass material. is there. Further, the weight ratio of the biomass resin is 51% by weight or more for the biomass material and 49% by weight or less for the thermoplastic resin from the viewpoint of increasing the generation of carbon dioxide accompanying the disposal and disposal as general household waste. It is desirable that

上記したように樹脂材料がポリエチレン樹脂のみである場合には、適正融解温度が170℃〜180℃であるが、5〜95重量%のバイオマス材料と5〜95重量%の熱可塑性樹脂からなるバイオマス樹脂である場合にはバイオマス材料の適正融解温度で融解することが好ましい。   When the resin material is only a polyethylene resin as described above, the proper melting temperature is 170 ° C. to 180 ° C., but the biomass is composed of 5 to 95 wt% biomass material and 5 to 95 wt% thermoplastic resin. When it is a resin, it is preferable to melt at an appropriate melting temperature of the biomass material.

例えば、5〜85重量%の米材料と15〜95重量%のポリエチレン樹脂からなるバイオマス樹脂である場合の融解温度は、米材料の適正融解温度である165℃〜170℃である。ポリエチレン樹脂と同じ融解温度170℃〜180℃だと粘性が低すぎてドローダウンが大きくなり、また165℃未満だと粘性が高すぎて成形不良を起こし完璧なブロー成形を行うことができない。   For example, the melting temperature in the case of a biomass resin composed of 5 to 85% by weight of rice material and 15 to 95% by weight of polyethylene resin is 165 ° C to 170 ° C, which is an appropriate melting temperature of rice material. When the melting temperature is 170 ° C. to 180 ° C., which is the same as that of the polyethylene resin, the viscosity is too low and the drawdown becomes large.

また、5〜85重量%の貝殻材料と15〜95重量%のポリエチレン樹脂からなるバイオマス樹脂である場合の融解温度は、貝殻材料の適正融解温度である180℃〜190℃である。ポリエチレン樹脂と同じ融解温度170℃〜180℃だと粘性が高すぎて成形不良を起こし完璧なブロー成形を行うことができず、また190℃以上だと粘性が低すぎてドローダウンが大きくなると共に、製造装置の負担が大きくなり好ましいものではない。   Moreover, the melting temperature in the case of the biomass resin which consists of 5-85 weight% shell material and 15-95 weight% polyethylene resin is 180 degreeC-190 degreeC which is an appropriate melting temperature of shell material. If the same melting temperature as polyethylene resin is 170 ° C to 180 ° C, the viscosity is too high to cause molding failure and perfect blow molding cannot be performed, and if it is 190 ° C or higher, the viscosity is too low and drawdown increases. This is not preferable because the burden on the manufacturing apparatus increases.

なお、バイオマス樹脂を構成するバイオマス材料は、米材料、貝殻材料に限定されるものではなく、トウモロコシ、サトウキビ等の粉末、杉等の木の大鋸屑であっても構わない。また、熱可塑性樹脂は、ポリエチレン樹脂に限定されるものではなく、ポリプロピレン樹脂であっても構わない。バイオマス樹脂でブロー成形されたマネキンMは、肉厚が2mm〜10mm程度であり、強度も充分備えており、しかもバイオマス材料特有の臭いや色が表現され、着色する必要がないので、興趣あるマネキンとして展示することができる。   In addition, the biomass material which comprises biomass resin is not limited to a rice material and a shell material, You may be large sawdust of trees, such as powders, such as corn and sugarcane, and cedar. Further, the thermoplastic resin is not limited to a polyethylene resin, and may be a polypropylene resin. Mannequin M blow-molded with biomass resin has a thickness of about 2 mm to 10 mm, has sufficient strength, expresses the smell and color peculiar to biomass materials, and does not need to be colored. Can be exhibited.

本願発明は、ブロー成形によってバイオマス樹脂からなるマネキンを製造する製造装置に利用可能である。   The present invention is applicable to a manufacturing apparatus for manufacturing a mannequin made of biomass resin by blow molding.

M マネキン
1 製造装置
2 ホッパー
3 口部
5 傾斜面
6 スクリュー内蔵管
7 スクリュー
9 駆動モータ
10 動力伝達手段
11 射出室
12 ダイス
13 隙間
16 金型(マネキン金型)
17 熔融中空体
19 前半体
20 後半体
21 マネキンの雌型
23 ノズル
25 挿通孔
M Mannequin 1 Manufacturing Equipment 2 Hopper 3 Portion 5 Inclined Surface 6 Screw Built-in Pipe 7 Screw 9 Drive Motor 10 Power Transmission Means 11 Injection Chamber 12 Die 13 Clearance 16 Mold (Mannequin Die)
17 Melted hollow body 19 First half body 20 Second half body 21 Female mannequin mold 23 Nozzle 25 Insertion hole

Claims (1)

ブロー成形によって製造するマネキンの製造方法であって、
5〜85重量%の貝殻材料と15〜95重量%のポリエチレン樹脂からなるバイオマス樹脂のペレットをホッパーからスクリュー内蔵管に送り、
スクリュー内蔵管内において前記バイオマス樹脂のペレットを加熱融解し、この融解したバイオマス樹脂をスクリューにて攪拌しつつ射出室内へ移送し、
射出室内においてバイオマス樹脂を貝殻材料の適正融解温度である180℃〜190℃まで加熱した後にマネキン金型内に射出して熔融中空体を形成し、
当該熔融中空体に圧縮空気を吹き込み、熔融中空体を膨張させてマネキン金型の内面に接触させ、
熔融中空体をマネキン金型の内面に接触させた状態で冷却固化させてマネキンを製造することを特徴とするマネキンの製造方法。
A manufacturing method of a mannequin manufactured by blow molding,
5-85 wt% of the shell material and the biomass resin pellets consisting of 15 to 95 wt% of a polyethylene resin feed from the hopper to the screw internal tube,
In the screw built-in tube, the biomass resin pellets are heated and melted, and the melted biomass resin is transferred to the injection chamber while stirring with a screw.
In the injection chamber, the biomass resin is heated to 180 ° C. to 190 ° C. which is an appropriate melting temperature of the shell material, and then injected into a mannequin mold to form a molten hollow body.
Compressed air is blown into the molten hollow body, the molten hollow body is expanded and brought into contact with the inner surface of the mannequin mold,
A mannequin manufacturing method comprising manufacturing a mannequin by cooling and solidifying a molten hollow body in contact with an inner surface of a mannequin mold.
JP2010069497A 2010-03-25 2010-03-25 Mannequin manufacturing method Active JP5350302B2 (en)

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JP7375320B2 (en) * 2019-03-28 2023-11-08 大日本印刷株式会社 Laminated bodies, lid materials and containers with lids

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JP2002010887A (en) * 2000-06-28 2002-01-15 Pearl Mannequin:Kk Biodegradable hollow mannequin
JP3706325B2 (en) * 2001-10-17 2005-10-12 株式会社シライ Mannequin body molding method
JP2006063301A (en) * 2004-04-08 2006-03-09 Kunio Matsubara Biodegradable resin composition derived from vegetable polymer starch and method for producing the same
JP5114651B2 (en) * 2006-10-18 2013-01-09 愛知県 POLYLACTIC ACID RESIN COMPOSITION, MOLDED ARTICLE, AND METHOD FOR PRODUCING THE SAME
JP3140103U (en) * 2007-12-21 2008-03-13 株式会社パールマネキン Mannequin made of biomass resin sheet

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* Cited by examiner, † Cited by third party
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