JP2007203502A - Thermoplastic resin made molded product and its manufacturing method - Google Patents

Thermoplastic resin made molded product and its manufacturing method Download PDF

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JP2007203502A
JP2007203502A JP2006022401A JP2006022401A JP2007203502A JP 2007203502 A JP2007203502 A JP 2007203502A JP 2006022401 A JP2006022401 A JP 2006022401A JP 2006022401 A JP2006022401 A JP 2006022401A JP 2007203502 A JP2007203502 A JP 2007203502A
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thermoplastic resin
mold
rib
molded product
foam sheet
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Akira Hanada
暁 花田
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Sumika Plastech Co Ltd
Sumitomo Chemical Co Ltd
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Sumika Plastech Co Ltd
Sumitomo Chemical Co Ltd
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<P>PROBLEM TO BE SOLVED: To provide a thermoplastic resin made molded product constituted by heat-sealing libs in part of a thermoplastic resin made foamed sheet and having good appearance and a producing method of the same. <P>SOLUTION: In the thermoplastic resin made molded product and the producing method of the same, the ribs 7 are heat-sealed to a part of the thermoplastic resin made foamed sheet 1, the shape of the ribs 7 satisfies 1 mm≤(V<SB>1</SB>/S<SB>1</SB>)≤9 mm, wherein V<SB>1</SB>is the volume (mm<SP>3</SP>) of the ribs and S<SB>1</SB>is the area (mm<SP>2</SP>) of the heat-sealed portions of the ribs. The thermoplastic resin made molded product is produced by supplying the softened thermoplastic resin made foamed sheet 1 between a shaping mold in whose shaping face recessed portions whose volume and area of opening portion satisfies 1 mm≤(V<SB>2</SB>/S<SB>2</SB>)≤9 mm, wherein V<SB>2</SB>is the volume of the recessed portion and S<SB>2</SB>is the area of the opening portion of the recessed portion, and a shaping mold which constitutes a pair along with the above shaping mold for shaping the ribs 7. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は熱可塑性樹脂製成形品およびその製造方法に関する。   The present invention relates to a thermoplastic resin molded article and a method for producing the same.

熱可塑性樹脂製発泡シートを成形して得られる成形品は、軽量性、リサイクル性、断熱性などに優れることから、自動車部材や建築材料等の種々の用途に用いられている。特に剛性が求められる用途では、発泡シートに部分的にリブを設けた成形品が使用される。このような発泡シートの一部にリブが融着されてなる熱可塑性樹脂製成形品の製造方法としては、所定形状に賦形してなる発泡積層シートに、部分的に溶融状の熱可塑性樹脂を供給して、リブを賦形する方法が知られている(例えば特許文献1参照)。   Molded articles obtained by molding a thermoplastic resin foam sheet are excellent in light weight, recyclability, heat insulation, and the like, and thus are used in various applications such as automobile members and building materials. Particularly in applications where rigidity is required, a molded product in which a rib is partially provided on a foamed sheet is used. As a method for producing a molded product made of a thermoplastic resin in which ribs are fused to a part of such a foamed sheet, a partially molten thermoplastic resin is formed into a foamed laminated sheet formed into a predetermined shape. Is known, and a rib is shaped (see, for example, Patent Document 1).

特開2003−231195号公報JP 2003-231195 A

リブによる補強効果は、賦形するリブの高さが高いほど、すなわち発泡シートからの突出具合の大きいほうが効果的である。特許文献1の方法によって高さの高いリブを有する熱可塑性樹脂製成形品を得るためには、該リブを賦形するための溶融状熱可塑性樹脂の供給圧力を高くする必要がある。しかしながら樹脂の供給圧力を高くすると、発泡シートのリブ融着部に圧力が集中して発泡シートを部分的に圧縮してしまい、得られる成形品に外観不良が生じることがあった。   The reinforcing effect by the ribs is more effective as the height of the ribs to be shaped is higher, that is, the larger the degree of protrusion from the foamed sheet. In order to obtain a thermoplastic resin molded product having a high rib by the method of Patent Document 1, it is necessary to increase the supply pressure of the molten thermoplastic resin for shaping the rib. However, when the supply pressure of the resin is increased, the pressure concentrates on the rib fused portion of the foam sheet, and the foam sheet is partially compressed, and the resulting molded product may have a poor appearance.

本発明は、熱可塑性樹脂製発泡シートの一部にリブが融着されてなる熱可塑性樹脂製成形品であって、外観良好な熱可塑性樹脂製成形品およびその製造方法を提供するものである。   The present invention provides a molded article made of a thermoplastic resin in which a rib is fused to a part of a foamed sheet made of a thermoplastic resin, and a molded article made of a thermoplastic resin having a good appearance and a method for producing the same. .

すなわち本発明は、熱可塑性樹脂製発泡シートの一部にリブが融着されてなる熱可塑性樹脂製成形品であって、該リブの形状が式(A)を満たす熱可塑性樹脂製成形品である。
1mm≦(V1/S1)≦9mm 式(A)
1:リブの体積(mm3
1:リブの融着部面積(mm2
また本発明は、以下の工程を順に含む、熱可塑性樹脂製発泡シートの一部にリブが融着されてなる前記熱可塑性樹脂製成形品の製造方法である。
(1)熱可塑性樹脂製発泡シートを加熱し軟化する工程
(2)前記リブを賦形するために、体積と開口部面積が式(B)を満たす凹部が成形面に形成された成形型Aと、該成形型Aと対を成す成形型Bとの間に、工程(1)で得られる熱可塑性樹脂製発泡シートを供給する工程
1mm≦(V2/S2)≦9mm 式(B)
2:凹部の体積(mm3
2:凹部の開口部面積(mm2
(3)成形型Aと成形型Bを型閉めし、熱可塑性樹脂製発泡シートを所定形状に賦形すると共に、成形型Aの成形面に形成された凹部の開口部を前記熱可塑性樹脂製発泡シートで塞ぐ工程
(4)該凹部に通ずるように成形型A内に設けられた樹脂通路を通じて溶融状熱可塑性樹脂を該凹部に供給し、該溶融状熱可塑性樹脂と前記熱可塑性樹脂製発泡シートとを融着一体化する工程
(5)溶融状熱可塑性樹脂の供給を停止すると同時または停止した後に、型開きして熱可塑性樹脂製成形品を取り出す工程
That is, the present invention relates to a thermoplastic resin molded product in which a rib is fused to a part of a thermoplastic resin foam sheet, and the shape of the rib satisfies the formula (A). is there.
1 mm ≦ (V 1 / S 1 ) ≦ 9 mm Formula (A)
V 1 : rib volume (mm 3 )
S 1 : Rib fused area (mm 2 )
Moreover, this invention is a manufacturing method of the said thermoplastic resin molded product which a rib is fuse | melted to a part of thermoplastic resin foam sheet which includes the following processes in order.
(1) Step of heating and softening the foamed sheet made of thermoplastic resin (2) Mold A in which a concave portion whose volume and opening area satisfy the formula (B) is formed on the molding surface in order to shape the rib And a step of supplying the thermoplastic resin foam sheet obtained in the step (1) between the mold A and the mold B paired with the mold A 1 mm ≦ (V 2 / S 2 ) ≦ 9 mm Formula (B)
V 2 : Volume of the recess (mm 3 )
S 2 : Opening area of the recess (mm 2 )
(3) The mold A and the mold B are closed, the thermoplastic resin foam sheet is shaped into a predetermined shape, and the opening of the recess formed on the molding surface of the mold A is made of the thermoplastic resin. Step 4 of closing with foam sheet (4) A molten thermoplastic resin is supplied to the concave portion through a resin passage provided in the mold A so as to communicate with the concave portion, and the molten thermoplastic resin and the thermoplastic resin foam are supplied. Step of fusing and integrating the sheet (5) Step of simultaneously opening or stopping the supply of the molten thermoplastic resin and then opening the mold to take out the molded product made of the thermoplastic resin

本発明の熱可塑性樹脂製成形品は、外観良好な成形品である。また本発明の熱可塑性樹脂製成形品の製造方法によれば、外観良好な熱可塑性樹脂製成形品を得ることができる。   The molded article made of the thermoplastic resin of the present invention is a molded article having a good appearance. Moreover, according to the method for producing a molded product of a thermoplastic resin of the present invention, a molded product of a thermoplastic resin having a good appearance can be obtained.

本発明は、熱可塑性樹脂製発泡シートの一部にリブが融着されてなる熱可塑性樹脂製成形品であって、該リブの形状が式(A)を満たす熱可塑性樹脂製成形品である。
1mm≦(V1/S1)≦9mm 式(A)
1:リブの体積(mm3
1:リブの融着部面積(mm2
The present invention is a molded product made of a thermoplastic resin in which a rib is fused to a part of a foamed sheet made of a thermoplastic resin, and the molded product made of a thermoplastic resin in which the shape of the rib satisfies the formula (A). .
1 mm ≦ (V 1 / S 1 ) ≦ 9 mm Formula (A)
V 1 : rib volume (mm 3 )
S 1 : Rib fused area (mm 2 )

ここでリブの体積とは、リブと熱可塑性樹脂製発泡シートとの融着部分で切断したときのリブの体積であり、リブの融着部面積とは、切断したリブにおける切断面の面積である。リブの体積V1と、リブと発泡シートとの融着部面積S1が式(A)を満たす本発明の熱可塑性樹脂製成形品は、発泡シートのリブ融着部が変形しておらず、外観良好な熱可塑性樹脂製発泡成形品である。本発明の熱可塑性樹脂製成形品におけるリブの位置や個数は特に限定されない。 Here, the volume of the rib is the volume of the rib when cut at the fused portion between the rib and the thermoplastic resin foam sheet, and the fused area of the rib is the area of the cut surface of the cut rib. is there. The volume V 1 of the ribs, the ribs and the expanded sheet and the thermoplastic resin molded article of the fused portion area S 1 is the invention which satisfies the formula (A) are not rib fused portion of the foam sheet is deformed It is a foamed product made of a thermoplastic resin with a good appearance. The position and the number of ribs in the thermoplastic resin molded article of the present invention are not particularly limited.

本発明におけるリブは、その高さHと、該リブと発泡シートとの融着部幅Wとが、以下の式(C)を満たすことが好ましい。
0.5≦(H/W)≦2 式(C)
リブの形状が式(C)を満たすようにすることにより、より外観良好な熱可塑性樹脂製成形品となる。なお、リブの高さHとは、発泡シートから切断されたリブにおける切断面からの最も高い高さであり、融着部幅Wとは、前記切断面において対向する辺間の最も短い長さである。
As for the rib in this invention, it is preferable that the height H and the fusion | melting part width W of this rib and a foam sheet satisfy | fill the following formula | equation (C).
0.5 ≦ (H / W) ≦ 2 Formula (C)
By making the rib shape satisfy the formula (C), a molded article made of a thermoplastic resin having a better appearance is obtained. The rib height H is the highest height from the cut surface of the rib cut from the foam sheet, and the fused portion width W is the shortest length between opposing sides in the cut surface. It is.

本発明の熱可塑性樹脂製成形品は、熱可塑性樹脂製発泡シートの一部にリブが融着されてなる。本発明で用いられる熱可塑性樹脂製発泡シートは特に限定されるものではないが、通常発泡倍率2〜10倍、厚さ1〜10mm程度の発泡シートが用いられる。また該熱可塑性樹脂製発泡シートには、真空成形、圧空成形、真空圧空成形、プレス成形などの方法により所望の形状を賦形することができる。   The thermoplastic resin molded article of the present invention is obtained by fusing ribs to a part of a thermoplastic resin foam sheet. Although the thermoplastic resin foam sheet used in the present invention is not particularly limited, a foam sheet having a foaming ratio of 2 to 10 times and a thickness of about 1 to 10 mm is usually used. In addition, the thermoplastic resin foam sheet can be formed into a desired shape by a method such as vacuum forming, pressure forming, vacuum pressure forming, press forming or the like.

本発明で用いる熱可塑性樹脂製発泡シートを構成する樹脂としては、エチレン、プロピレン、ブテン、ペンテン、ヘキセン等の炭素原子数が2〜6のオレフィンホモポリマーや、炭素原子数が2〜10のオレフィンから選択される2種類以上のモノマーを共重合して得られるオレフィン共重合体などのオレフィン系樹脂、エチレン−ビニルエステル共重合体、エチレン−(メタ)アクリル酸共重合体、エチレン−(メタ)アクリル酸エステル共重合体、エステル系樹脂、アミド系樹脂、スチレン系樹脂、アクリル系樹脂、アクリロニトリル系樹脂、アイオノマー樹脂などがあげられる。これらの樹脂は単独で使用してもよく、複数の樹脂を併用してもよい。成形性、耐油性、コストなどの観点からオレフィン系樹脂が好ましく用いられ、得られる成形品の剛性、耐熱性などの観点からプロピレン系樹脂が特に好ましく用いられる。   Examples of the resin constituting the thermoplastic resin foam sheet used in the present invention include olefin homopolymers having 2 to 6 carbon atoms such as ethylene, propylene, butene, pentene, and hexene, and olefins having 2 to 10 carbon atoms. Olefin resins such as olefin copolymers obtained by copolymerizing two or more monomers selected from ethylene, ethylene-vinyl ester copolymers, ethylene- (meth) acrylic acid copolymers, ethylene- (meth) Examples include acrylic ester copolymers, ester resins, amide resins, styrene resins, acrylic resins, acrylonitrile resins, and ionomer resins. These resins may be used alone or in combination with a plurality of resins. Olefin resins are preferably used from the viewpoints of moldability, oil resistance, cost, etc., and propylene resins are particularly preferably used from the viewpoint of rigidity and heat resistance of the obtained molded product.

プロピレン系樹脂としては、プロピレンホモポリマーや、プロピレン由来のモノマー単位を50モル%以上含むプロピレン系共重合体をあげることができる。共重合体は、ブロック共重合体、ランダム共重合体、グラフト共重合体のいずれでもよい。好ましく用いられるプロピレン系共重合体の例としては、エチレンまたは炭素原子数4〜10のα−オレフィンとプロピレンとの共重合体を挙げることができる。炭素原子数4〜10のα−オレフィンとしては、例えば、1−ブテン、4−メチルペンテン−1、1−ヘキセンおよび1−オクテンが挙げられる。プロピレン系共重合体中のプロピレン以外のモノマー単位の含有量は、エチレンについては15モル%以下、炭素原子数4〜10のα−オレフィンについては30モル%以下であることが好ましい。プロピレン系樹脂は1種類でもよく、2種類以上を混合して用いてもよい。   Examples of the propylene resin include propylene homopolymers and propylene copolymers containing 50 mol% or more of monomer units derived from propylene. The copolymer may be any of a block copolymer, a random copolymer, and a graft copolymer. As an example of the propylene copolymer preferably used, a copolymer of ethylene or an α-olefin having 4 to 10 carbon atoms and propylene can be given. Examples of the α-olefin having 4 to 10 carbon atoms include 1-butene, 4-methylpentene-1, 1-hexene and 1-octene. The content of monomer units other than propylene in the propylene-based copolymer is preferably 15 mol% or less for ethylene and 30 mol% or less for α-olefins having 4 to 10 carbon atoms. One type of propylene resin may be used, or two or more types may be mixed and used.

長鎖分岐プロピレン系樹脂や重量平均分子量が1×105以上の高分子量プロピレン系樹脂を、発泡層を構成する熱可塑性樹脂の50重量%以上用いることにより、微細な気泡を有するプロピレン系樹脂発泡シートを得ることができる。さらにこのようなプロピレン系樹脂の中でも、シートリサイクル時にゲルを生じにくいことから非架橋のプロピレン系樹脂が好ましく使用される。 By using 50% by weight or more of the thermoplastic resin constituting the foam layer of a long-chain branched propylene resin or a high molecular weight propylene resin having a weight average molecular weight of 1 × 10 5 or more, a propylene resin foam having fine bubbles is used. A sheet can be obtained. Further, among such propylene resins, non-crosslinked propylene resins are preferably used because gels are unlikely to occur during sheet recycling.

ここで長鎖分岐プロピレン系樹脂とは、分岐度指数[A]が0.20≦[A]≦0.98を満たすプロピレン系樹脂を指す。
分岐度指数[A]が0.20≦[A]≦0.98を満たす長鎖分岐プロピレン系樹脂の例としては、バゼル社製のプロピレンPF−814が挙げられる。
Here, the long-chain branched propylene-based resin refers to a propylene-based resin having a degree of branching index [A] satisfying 0.20 ≦ [A] ≦ 0.98.
An example of a long-chain branched propylene-based resin satisfying the branching index [A] of 0.20 ≦ [A] ≦ 0.98 is propylene PF-814 manufactured by Basel.

分岐度指数とは、重合体における長鎖分岐の程度を示すものであり、下記の式において定義される数値である。
分岐度指数 [A] =〔η〕Br/〔η〕Lin
ここで〔η〕Brは、長鎖分岐を有するプロピレン系樹脂の固有粘度であり、〔η〕Linは、該長鎖分岐を有するプロピレン系樹脂と同じモノマー単位および同じ重量平均分子量を有する、直鎖プロピレン系樹脂の固有粘度である。
固有粘度は極限粘度数とも呼ばれ、重合体の溶液粘度を増強する能力の尺度である。固有粘度は特にポリマー分子の分子量と、分岐度に依存する。したがって、長鎖分岐を有するポリマーの固有粘度と、該長鎖分岐を有するポリマーと同じ重量平均分子量の直鎖ポリマーの固有粘度とを比較することにより、該長鎖分岐を有するポリマーの分岐度の尺度とすることができる。プロピレン系樹脂の固有粘度の測定方法は、エリオット等[J.Appl.Polym.Sci.,14,2947−2963(1970)]により開示されているような従来知られている方法により測定することができ、例えば、プロピレン系樹脂をテトラリン又はオルトジクロロベンゼンに溶解し、135℃で固有粘度を測定することが可能である。
プロピレン系樹脂の重量平均分子量(Mw)は、通常用いられる種々の方法で測定できるが、M.L.McConnelによって、American Laboratory,May,63−75(1978)に発表されている方法、即ち、低角度レーザー光散乱強度測定法が特に好ましく用いられる。
重量平均分子量が1×105以上の高分子量プロピレン系樹脂を重合する方法の例としては、特開平11−228629号公報に記載されたように、まず高分子量成分を重合した後に続いて低分子量成分を重合する方法などがあげられる。
The degree of branching index indicates the degree of long chain branching in a polymer, and is a numerical value defined in the following formula.
Branch index [A] = [η] Br / [η] Lin
Here, [η] Br is the intrinsic viscosity of the propylene resin having a long chain branch, and [η] Lin is a straight chain having the same monomer unit and the same weight average molecular weight as the propylene resin having the long chain branch. It is an intrinsic viscosity of a chain propylene resin.
Intrinsic viscosity, also called intrinsic viscosity, is a measure of the ability of a polymer to enhance solution viscosity. Intrinsic viscosity depends in particular on the molecular weight of the polymer molecules and the degree of branching. Therefore, by comparing the intrinsic viscosity of a polymer having long chain branches with the intrinsic viscosity of a linear polymer having the same weight average molecular weight as that of the polymer having long chain branches, the degree of branching of the polymer having long chain branches can be determined. It can be a scale. The method for measuring the intrinsic viscosity of a propylene-based resin is described by Elliott et al. [J. Appl. Polym. Sci. , 14, 2947-2963 (1970)], for example, a propylene resin is dissolved in tetralin or orthodichlorobenzene, and the intrinsic viscosity at 135 ° C. Can be measured.
The weight average molecular weight (Mw) of the propylene-based resin can be measured by various commonly used methods. L. The method disclosed by McConnel in American Laboratory, May, 63-75 (1978), that is, a low-angle laser light scattering intensity measurement method is particularly preferably used.
As an example of a method for polymerizing a high molecular weight propylene resin having a weight average molecular weight of 1 × 10 5 or more, as described in JP-A No. 11-228629, a high molecular weight component is first polymerized, followed by low molecular weight. Examples thereof include a method of polymerizing components.

長鎖分岐プロピレン系樹脂または高分子量プロピレン系樹脂の中でも、融点+30℃付近において下記の条件で測定した一軸溶融伸張粘度比η5/η0.1が5以上であるプロピレン系樹脂が好ましく、より好ましくは10以上の樹脂である。一軸溶融伸張粘度比とは、伸張ひずみ速度1sec-1で、一軸伸張粘度測定装置(例としてレオメトリックス社製一軸伸張粘度測定装置などがあげられる)などの装置を用いて測定される値であり、歪み開始から0.1秒後の一軸溶融伸長粘度をη0.1とし、5秒後の一軸溶融伸張粘度をη5とする。このような一軸伸張粘度特性を有するプロピレン系樹脂を使用することによって、より微細な気泡を有する発泡シートを製造することができる。 Among long-chain branched propylene resins or high-molecular-weight propylene resins, propylene resins having a uniaxial melt-extension viscosity ratio η 5 / η 0.1 measured under the following conditions at around melting point + 30 ° C. are preferably 5 or more, more preferably 10 or more resins. The uniaxial melt extensional viscosity ratio is a value measured using an apparatus such as a uniaxial extensional viscosity measurement apparatus (for example, a uniaxial extensional viscosity measurement apparatus manufactured by Rheometrics, Inc.) at an elongation strain rate of 1 sec −1 . the uniaxial melt elongation viscosity after 0.1 seconds from the strain initiation and eta 0.1, the uniaxial melt elongation viscosity after 5 seconds and eta 5. By using a propylene-based resin having such uniaxial extensional viscosity characteristics, a foam sheet having finer bubbles can be produced.

熱可塑性樹脂製発泡シートを製造する際に使用される発泡剤は、いわゆる化学発泡剤および物理発泡剤のいずれでもよく、これらを併用してもよい。上記化学発泡剤としては、例えば分解されて窒素ガスを発生する熱分解型発泡剤(アゾジカルボンアミド、アゾビスイソブチロニトリル、ジニトロソペンタメチレンテトラミン、p−トルエンスルホニルヒドラジド、p,p’−オキシ−ビス(ベンゼンスルホニルヒドラジド)など)、分解されて炭酸ガスを発生する熱分解型無機発泡剤(炭酸水素ナトリウム、炭酸アンモニウム、炭酸水素アンモニウムなど)など公知の熱分解型発泡性化合物が挙げられる。物理発泡剤としては、具体的にはプロパン、ブタン、水、炭酸ガス等があげられる。上記例示の発泡剤のうち取扱いが容易であることから熱分解型発泡剤が特に好ましく用いられ、発泡倍率の高い発泡シートを形成させやすいことから、アゾジカルボンアミドと炭酸水素ナトリウムの混合物が特に好ましく用いられる。発泡シートを構成する樹脂への発泡剤の配合方法としては、樹脂ペレットと発泡剤マスターバッチペレットをドライブレンドした後、押出機に供給し、押出機内で樹脂を可塑化させ、ダイス出口から樹脂を押出しながら発泡させて発泡シートを形成する方法が好ましく用いられる。発泡剤の使用量は所望の発泡倍率が得られるように、用いる発泡剤や樹脂の種類に応じて適宜選択されるものであり、通常熱可塑性樹脂100重量部に対して発泡剤0.5〜20重量部である。   The foaming agent used in producing the thermoplastic resin foam sheet may be either a so-called chemical foaming agent or a physical foaming agent, or a combination thereof. Examples of the chemical foaming agent include a thermal decomposition type foaming agent that decomposes to generate nitrogen gas (azodicarbonamide, azobisisobutyronitrile, dinitrosopentamethylenetetramine, p-toluenesulfonylhydrazide, p, p'- Oxy-bis (benzenesulfonyl hydrazide) and the like, and pyrolytic inorganic foaming agents that decompose to generate carbon dioxide (sodium hydrogen carbonate, ammonium carbonate, ammonium bicarbonate, etc.) . Specific examples of the physical foaming agent include propane, butane, water, carbon dioxide gas, and the like. Among the foaming agents exemplified above, a pyrolytic foaming agent is particularly preferably used because it is easy to handle, and a mixture of azodicarbonamide and sodium hydrogencarbonate is particularly preferred because it is easy to form a foam sheet having a high expansion ratio. Used. As a method of blending the foaming agent into the resin constituting the foamed sheet, the resin pellets and the foaming agent master batch pellet are dry blended, then supplied to the extruder, the resin is plasticized in the extruder, and the resin is discharged from the die outlet. A method of forming a foamed sheet by foaming while extruding is preferably used. The amount of the foaming agent used is appropriately selected according to the type of foaming agent and resin used so that a desired foaming ratio can be obtained. 20 parts by weight.

熱可塑性樹脂製発泡シートの製造方法は特に限定されるものではないが、フラットダイ(Tダイ)やサーキュラーダイを用いた押出成形により得られたシートが好ましく、サーキュラーダイから溶融した樹脂を発泡させながら押出し、マンドレル等に沿わせて延伸、冷却を行なう方法が特に好ましく用いられる。発泡シートを押出成形により製造する場合には、溶融した樹脂をダイから押出し冷却固化させた後に延伸を行なうこともできる。発泡シートは単層であっても多層であってもよいが、シート製造時の破泡を防止する観点から、非発泡層を両外層に有する多層構成の発泡シートが好ましい。非発泡層を構成する樹脂は、発泡層を構成する樹脂の例として前記したものを使用することができるが、発泡層を構成する樹脂と同種類のものであるものが好ましく、例えば発泡層がプロピレン系樹脂である場合、非発泡層もプロピレン系樹脂で構成されることが好ましい。非発泡層の厚さは発泡層の1〜10%であることが好ましく、軽量性と剛性のバランスからは2〜5%であることが好ましい。   The method for producing the thermoplastic resin foam sheet is not particularly limited, but a sheet obtained by extrusion molding using a flat die (T-die) or a circular die is preferable, and the resin melted from the circular die is foamed. However, a method of stretching and cooling along extrusion, mandrels and the like is particularly preferably used. When the foamed sheet is produced by extrusion molding, the molten resin can be extruded from a die and solidified by cooling and then stretched. The foamed sheet may be a single layer or a multilayer, but from the viewpoint of preventing foam breakage during sheet production, a multilayered foam sheet having non-foamed layers in both outer layers is preferred. As the resin constituting the non-foamed layer, those described above as examples of the resin constituting the foamed layer can be used, but the same type of resin as that constituting the foamed layer is preferable. In the case of a propylene-based resin, the non-foamed layer is also preferably composed of a propylene-based resin. The thickness of the non-foamed layer is preferably 1 to 10% of the foamed layer, and is preferably 2 to 5% from the balance between lightness and rigidity.

本発明で用いる熱可塑性樹脂製発泡シートは、単層または多層の発泡シートとその他の材料とを貼合した複合シートであってもよい。このような複合シートは、発泡シートと他の材料とをドライラミネーション、サンドラミネーション、熱ロール貼合、熱風貼合などにより貼り合わせることにより得られる。
発泡シートと積層する他の材料としては、織布、不織布、シート、フィルム、発泡体、網状物などが挙げられる。これらの材料はオレフィン系樹脂、塩化ビニル系樹脂、スチレン系樹脂などの熱可塑性樹脂、ポリブタジエン、エチレン−プロピレン共重合体などのゴムや熱可塑性エラストマー、綿、麻、竹などのセルロース系繊維などが挙げられる。これらの材料にはシボなどの凹凸模様、印刷や染色が施されていてもよく、単層であっても多層であってもよい。
The thermoplastic resin foam sheet used in the present invention may be a composite sheet obtained by laminating a single layer or multilayer foam sheet and other materials. Such a composite sheet is obtained by laminating a foam sheet and another material by dry lamination, sand lamination, hot roll bonding, hot air bonding, or the like.
Examples of other materials laminated with the foam sheet include woven fabric, nonwoven fabric, sheet, film, foam, and net-like material. These materials include thermoplastic resins such as olefin resins, vinyl chloride resins, and styrene resins, rubbers such as polybutadiene and ethylene-propylene copolymers, thermoplastic elastomers, and cellulose fibers such as cotton, hemp, and bamboo. Can be mentioned. These materials may be provided with an uneven pattern such as a texture, printed or dyed, and may be a single layer or a multilayer.

本発明におけるリブを形成する熱可塑性樹脂としては、前述の熱可塑性樹脂製発泡シートを形成する樹脂と同様の樹脂を使用することができる。成形性、耐油性、コストなどの観点からオレフィン系樹脂が好ましく用いられ、剛性、耐熱性などの観点からプロピレン系樹脂が特に好ましく用いられる。プロピレン系樹脂を用いる場合は、成形時の樹脂の流動性や、賦形されたリブの強度の点から、メルトフローレートが50〜300g/10min程度の樹脂が好ましく用いられる。   As the thermoplastic resin forming the rib in the present invention, the same resin as the resin forming the thermoplastic resin foam sheet can be used. Olefin resins are preferably used from the viewpoints of moldability, oil resistance, cost, and the like, and propylene resins are particularly preferably used from the viewpoint of rigidity, heat resistance, and the like. When a propylene-based resin is used, a resin having a melt flow rate of about 50 to 300 g / 10 min is preferably used from the viewpoint of the fluidity of the resin during molding and the strength of the shaped rib.

本発明の熱可塑性樹脂製発泡シートやリブは、添加剤を含有していてもよい。添加剤としては、充填剤(フィラー)、酸化防止剤、光安定剤、紫外線吸収剤、可塑剤、帯電防止剤、着色剤、剥離剤、流動性付与剤、滑剤などがあげられる。上記添加剤の例としては、具体的にはガラス繊維、カーボン繊維等の無機繊維、タルク、クレー、シリカ、酸化チタン、炭酸カルシウム、硫酸マグネシウム等の無機粒子等があげられる。これらの中でも、発泡シートやリブの強度向上や、成形時の収縮率を低下させる観点からタルクやガラス繊維などを5〜30wt%程度配合することが好ましい。   The thermoplastic resin foam sheet or rib of the present invention may contain an additive. Examples of the additive include a filler (filler), an antioxidant, a light stabilizer, an ultraviolet absorber, a plasticizer, an antistatic agent, a colorant, a release agent, a fluidity-imparting agent, and a lubricant. Specific examples of the additive include inorganic fibers such as glass fibers and carbon fibers, inorganic particles such as talc, clay, silica, titanium oxide, calcium carbonate, and magnesium sulfate. Among these, it is preferable to mix about 5 to 30 wt% of talc, glass fiber, etc. from the viewpoint of improving the strength of the foamed sheet or rib and reducing the shrinkage rate during molding.

本発明の熱可塑性樹脂製成形品の製造方法としては、以下の工程を順に含む製造方法が挙げられる。
(1)熱可塑性樹脂製発泡シートを加熱し軟化する工程
(2)前記リブを賦形するために、体積と開口部面積が式(B)を満たす凹部が成形面に形成された成形型Aと、該成形型Aと対を成す成形型Bとの間に、工程(1)で得られる熱可塑性樹脂製発泡シートを供給する工程
1mm≦(V2/S2)≦9mm 式(B)
2:凹部の体積(mm3
2:凹部の開口部面積(mm2
(3)成形型Aと成形型Bを型閉めし、熱可塑性樹脂製発泡シートを所定形状に賦形すると共に、成形型Aの成形面に形成された凹部の開口部を前記熱可塑性樹脂製発泡シートで塞ぐ工程
(4)該凹部に通ずるように成形型A内に設けられた樹脂通路を通じて溶融状熱可塑性樹脂を該凹部に供給し、該溶融状熱可塑性樹脂と前記熱可塑性樹脂製発泡シートとを融着一体化する工程
(5)溶融状熱可塑性樹脂の供給を停止すると同時または停止した後に、型開きして熱可塑性樹脂製成形品を取り出す工程
As a manufacturing method of the thermoplastic resin molded article of the present invention, a manufacturing method including the following steps in order is mentioned.
(1) Step of heating and softening the foamed sheet made of thermoplastic resin (2) Mold A in which a concave portion whose volume and opening area satisfy the formula (B) is formed on the molding surface in order to shape the rib And a step of supplying the thermoplastic resin foam sheet obtained in the step (1) between the mold A and the mold B paired with the mold A 1 mm ≦ (V 2 / S 2 ) ≦ 9 mm Formula (B)
V 2 : Volume of the recess (mm 3 )
S 2 : Opening area of the recess (mm 2 )
(3) The mold A and the mold B are closed, the thermoplastic resin foam sheet is shaped into a predetermined shape, and the opening of the recess formed on the molding surface of the mold A is made of the thermoplastic resin. Step 4 of closing with foam sheet (4) A molten thermoplastic resin is supplied to the concave portion through a resin passage provided in the mold A so as to communicate with the concave portion, and the molten thermoplastic resin and the thermoplastic resin foam are supplied. Step of fusing and integrating the sheet (5) Step of simultaneously opening or stopping the supply of the molten thermoplastic resin and then opening the mold to take out the molded product made of the thermoplastic resin

前記熱可塑性樹脂製成形品の製造方法においては、賦形するリブの形状や個数に応じた凹部が形成されてなる成形面を有する成形型Aと、該成形型Aと対を成す成形型Bとを用いる。成形型Aに設けられた凹部は、式(B)を満たす。凹部を有する成形型内には、前記凹部に溶融状熱可塑性樹脂を供給するための樹脂通路が設けられている。該樹脂通路から、式(B)を満たす凹部に溶融状熱可塑性樹脂を供給することにより、低い圧力で溶融状熱可塑性樹脂を供給することができるため、熱可塑性樹脂製発泡シートの変形を抑制することができ、外観良好な熱可塑性樹脂製成形品を得ることができる。成形型A、Bは、一方が雄型で他方が雌型であってもよく、両方が雌型、または両方が板状成形型であってもよい。また、成形型Bの成形面にもリブを賦形するための凹部が形成されていてもよい。   In the method for producing a thermoplastic resin molded product, a molding die A having a molding surface formed with recesses corresponding to the shape and number of ribs to be shaped, and a molding die B that forms a pair with the molding die A And are used. The recess provided in the mold A satisfies the formula (B). A resin passage for supplying molten thermoplastic resin to the recess is provided in the mold having the recess. The molten thermoplastic resin can be supplied at a low pressure by supplying the molten thermoplastic resin to the recess satisfying the formula (B) from the resin passage, so that the deformation of the thermoplastic resin foam sheet is suppressed. And a molded article made of a thermoplastic resin having a good appearance can be obtained. One of the molds A and B may be a male mold and the other a female mold, both may be female molds, or both may be plate-shaped molds. Moreover, the recessed part for shaping a rib may be formed also in the molding surface of the shaping | molding die B. FIG.

成形型の材質は特に限定されるものではないが、寸法安定性、耐久性などの観点から通常金属製であり、コストや軽量性などの面からアルミ製やステンレス製であることが好ましい。また成形型は、ヒーターや熱媒などにより温度調整可能な構造であることが好ましい。成形型は、成形時にはその成形面を30〜80℃とすることが好ましく、50〜60℃とすることがさらに好ましい。   The material of the mold is not particularly limited, but is usually made of metal from the viewpoint of dimensional stability and durability, and is preferably made of aluminum or stainless steel from the viewpoint of cost and light weight. Moreover, it is preferable that a shaping | molding die is a structure which can adjust temperature with a heater, a heat medium, etc. The molding die preferably has a molding surface of 30 to 80 ° C., more preferably 50 to 60 ° C. during molding.

以下、本発明の熱可塑性樹脂製成形品の製造方法の例を図1に基づき説明する。図1−(1)は加熱軟化された熱可塑性樹脂製発泡シートを、式(B)を満たす形状の凹部が成形面に形成された平板状の成形型Aと、平板状の成形型Bとの間に、熱可塑性樹脂製発泡シートを供給する工程(2)を示している。
図1−(2)は、成形型Aと成形型Bを型閉めし、熱可塑性樹脂製発泡シートを所定形状に賦形する工程(3)である。熱可塑性樹脂製発泡シートを賦形する方法としては、真空成形、圧空成形、真空圧空成形、プレス成形が挙げられる。複雑な形状にも容易に賦形できることから、真空成形、圧空成形、真空圧空成形が特に好ましく適用される。これらの方法で熱可塑性樹脂製発泡シートを賦形する場合には、成形型A、Bの少なくとも一方に、その成形面から真空吸引または圧縮空気の供給が可能な型を用いる。具体的には、成形型Aが真空吸引可能、成形型AとBの両方が真空吸引可能、成形型Bが圧縮空気の供給が可能、成形型Aが真空吸引可能で成形型Bが圧縮空気の供給が可能、といった組合せがあげられる。真空吸引または圧縮空気の供給が可能な型としては、成形型の成形面の少なくとも一部が焼結合金から構成される型や、成形面の少なくとも一部に孔が設けられた型等が挙げられる。成形型に設けられる孔の数や位置、孔径は特に限定されるものではない。
Hereinafter, an example of a method for producing a thermoplastic resin molded article of the present invention will be described with reference to FIG. FIG. 1- (1) shows a heat-softened foam sheet made of a thermoplastic resin, a flat plate-shaped mold A in which concave portions having a shape satisfying the formula (B) are formed on the molding surface, and a flat plate-shaped mold B The process (2) which supplies a thermoplastic resin foam sheet is shown.
FIG. 1- (2) shows a step (3) in which the mold A and the mold B are closed and the thermoplastic resin foam sheet is shaped into a predetermined shape. Examples of the method for shaping the thermoplastic resin foam sheet include vacuum forming, pressure forming, vacuum / pressure forming, and press forming. Since complex shapes can be easily formed, vacuum forming, pressure forming, and vacuum / pressure forming are particularly preferably applied. When the thermoplastic resin foam sheet is shaped by these methods, a mold that can be vacuum-sucked or supplied with compressed air from its molding surface is used as at least one of the molds A and B. Specifically, the mold A can be vacuumed, both the molds A and B can be vacuumed, the mold B can be supplied with compressed air, the mold A can be vacuumed, and the mold B can be compressed air. Can be supplied. Examples of the mold capable of vacuum suction or supply of compressed air include a mold in which at least a part of the molding surface of the molding die is made of a sintered alloy, a mold in which holes are provided in at least a part of the molding surface, and the like. It is done. The number and position of holes provided in the mold and the hole diameter are not particularly limited.

真空成形により熱可塑性樹脂製発泡シートを賦形する場合には、型閉めすると同時または型閉め終了後に成形型成形面から真空吸引を開始し、前記熱可塑性樹脂製発泡シートを成形型成形面に密着させ所定形状に賦形する。真空吸引は成形型Aからのみ行ってもよく、両成形型から行なってもよい。両成形型から真空吸引を行う場合、真空吸引の開始は同時でもよく、いずれか一方から先に真空吸引を開始してもよい。両成形型から真空吸引を行なう場合は、各成形型の成形面と熱可塑性樹脂製発泡シートとが密着した状態を維持しながら型開きしてもよい。この方法により、発泡倍率の高い熱可塑性樹脂製成形品を得ることができる。なお型開きは、凹部に溶融状熱可塑性樹脂を供給した後、あるいは供給しながら行なってもよい。真空吸引の程度は特に限定されるものではないが、成形型と発泡シートとの間の真空度が−0.05〜0.1MPaとなるように真空吸引することが好ましい。真空度とは、大気圧に対する成形型と発泡シートとの間の圧である。すなわち「真空度が−0.05MPa」とは、大気圧に対する成形型と発泡シートとの間の圧力が0.95MPaであることを示す。大気圧に対する成形型と発泡シートとの間の圧の真空度とは、成形型内の真空吸引用通路において測定される。   When forming a thermoplastic resin foam sheet by vacuum molding, vacuum suction is started from the molding surface at the same time when the mold is closed or after the mold is closed, and the thermoplastic foam sheet is applied to the molding surface. Adhere to a predetermined shape. Vacuum suction may be performed only from the mold A or from both molds. When vacuum suction is performed from both molds, the vacuum suction may be started simultaneously, or the vacuum suction may be started first from either one. When vacuum suction is performed from both molds, the molds may be opened while maintaining a state in which the molding surfaces of the molds and the thermoplastic resin foam sheet are in close contact with each other. By this method, a molded article made of a thermoplastic resin having a high expansion ratio can be obtained. The mold opening may be performed after supplying the molten thermoplastic resin to the recess or while supplying the molten thermoplastic resin. The degree of vacuum suction is not particularly limited, but vacuum suction is preferably performed so that the degree of vacuum between the mold and the foamed sheet is −0.05 to 0.1 MPa. The degree of vacuum is the pressure between the mold and the foam sheet with respect to atmospheric pressure. That is, “the degree of vacuum is −0.05 MPa” indicates that the pressure between the mold and the foamed sheet with respect to atmospheric pressure is 0.95 MPa. The degree of vacuum of the pressure between the mold and the foamed sheet with respect to atmospheric pressure is measured in a vacuum suction passage in the mold.

圧空成形により熱可塑性樹脂製発泡シートを所定形状に賦形する場合には、圧縮空気を成形型Bと熱可塑性樹脂製発泡シートとの間の加圧度が2〜5MPa程度となるように供給することが好ましい。成形型Aと熱可塑性樹脂製発泡シートとの間の加圧度は、成形型内の圧縮空気供給通路において測定される圧力である。
図1−(2)では、型閉めにより熱可塑性樹脂製発泡シートが成形型成形面と接して賦形されるため、成形型成形面に設けられた凹部の開口部が熱可塑性樹脂製発泡シートにより塞がれた状態となる。
When a thermoplastic resin foam sheet is shaped into a predetermined shape by pressure forming, compressed air is supplied so that the pressure between the mold B and the thermoplastic resin foam sheet is about 2 to 5 MPa. It is preferable to do. The degree of pressurization between the mold A and the thermoplastic resin foam sheet is a pressure measured in the compressed air supply passage in the mold.
In FIG. 1- (2), since the thermoplastic resin foam sheet is formed in contact with the molding surface of the mold by closing the mold, the opening of the recess provided in the molding surface of the mold is the thermoplastic resin foam sheet. It will be in the state blocked by.

図1−(3)は、該凹部に通ずるように成形型A内に設けられた樹脂通路を通じて溶融状熱可塑性樹脂を該凹部に供給し、溶融状熱可塑性樹脂と前記熱可塑性樹脂製発泡シートとを融着一体化する工程(4)である。溶融状熱可塑性樹脂は供給時の樹脂圧力が低いほど融着時に熱可塑性樹脂製発泡シートに外観不良を生じにくい。溶融状熱可塑性樹脂の金型キャビティ内の最大圧力は5MPa以下であることが好ましく、さらに溶融状熱可塑性樹脂供給時に成形型と熱可塑性樹脂製発泡シートの接触面から溶融状熱可塑性樹脂が漏れてバリ発生することによる外観不良を低減させるためには、3MPa以下であることがより好ましい。工程(3)で真空成形によって熱可塑性樹脂製発泡シートを成形する場合には、工程(4)で凹部に溶融情熱可塑性樹脂を供給する際にも、真空吸引を継続していてもよい。図1−(3)は、溶融状熱可塑性樹脂と熱可塑性樹脂製発泡シートとが融着一体化された状態を示している。   FIG. 1- (3) shows a state where molten thermoplastic resin is supplied to the concave portion through a resin passage provided in the mold A so as to communicate with the concave portion, and the molten thermoplastic resin and the thermoplastic resin foam sheet are supplied. (4). As the molten thermoplastic resin has a lower resin pressure at the time of supply, the appearance of the thermoplastic resin foam sheet is less likely to occur during fusion. The maximum pressure in the mold cavity of the molten thermoplastic resin is preferably 5 MPa or less, and when the molten thermoplastic resin is supplied, the molten thermoplastic resin leaks from the contact surface between the mold and the thermoplastic resin foam sheet. In order to reduce appearance defects due to the occurrence of burrs, the pressure is more preferably 3 MPa or less. When the thermoplastic resin foam sheet is formed by vacuum forming in the step (3), the vacuum suction may be continued when the molten passion plastic resin is supplied to the recesses in the step (4). FIG. 1- (3) shows a state in which a molten thermoplastic resin and a thermoplastic resin foam sheet are fused and integrated.

工程(5)は、溶融状熱可塑性樹脂の供給を停止すると同時または停止した後に、型開きして熱可塑性樹脂発泡成形品を取り出す工程である。図1−(4)は、型開きした状態を示している。 The step (5) is a step of taking out the thermoplastic resin foam molded product by opening the mold simultaneously with or after stopping the supply of the molten thermoplastic resin. FIG. 1- (4) shows a state where the mold is opened.

本発明の熱可塑性樹脂製成形品は、食品容器などの包装材料や、自動車内装部品、建築材料、家電製品などに使用することができる。自動車内装部品の例としてはドアトリム、天井、トランクサイドなどが挙げることができる。   The molded product of the thermoplastic resin of the present invention can be used for packaging materials such as food containers, automobile interior parts, building materials, and home appliances. Examples of automobile interior parts include door trims, ceilings, and trunk sides.

以下、本発明を実施例に基づき説明するが、本発明は実施例に何ら限定されるものではない。
[実施例1]
EXAMPLES Hereinafter, although this invention is demonstrated based on an Example, this invention is not limited to an Example at all.
[Example 1]

発泡倍率3倍、厚み3mmのポリプロピレン発泡シート(住化プラステック製 商品名スミセラー発泡PPシート)を用いて、図1に示す方法で熱可塑性樹脂製成形品を製造した。
リブを形成するための凹部(5)(図2に示すような、凹部の開口部厚み(9)5mm、反開口部厚み(10)4mm、高さ(11)5mm、長さ(12)370mm、体積(13)8325mm3、凹部の開口部面積(14)1850mm2の形状を有する)を成形面に有する成形型A(3)と、平板形状に賦形できる成形型B(6)からなる一対の金型を使用し、リブを有する平板の成形を行った。成形型Aは、その内部に、前記凹部に通ずるように溶融状熱可塑性樹脂を供給可能な樹脂通路(4)が設けられ、樹脂通路の凹部付近に溶融状熱可塑性樹脂圧力測定用センサーを備えた型であった。成形型A(3)は60℃に温度調整して用いた。
熱可塑性樹脂製発泡シート(1)を、押出機を備えた真空成形機(佐藤鉄工製VAIM0301)のクランプ枠(2)に固定した状態で近赤外ヒーターによりシートの上表面が190℃になるように加熱し軟化させた。加熱軟化させた発泡シート(1)を、クランプ枠(2)で固定した状態で、成形型A(3)と成形型B(6)との間に供給した。
次に成形型A(3)と成形型B(6)を型閉めし、プレス成形により厚さ2.8mmの平板状熱可塑性樹脂製成形品に賦形した。
プロピレン系樹脂(住友化学製ポリプロピレン、ノーブレンBUE81E6、MFR=80g/min)を、成形型A(3)内の樹脂通路(4)を通じて、3g/secで成形型凹部に2.5秒間供給し、前記凹部を溶融状熱可塑性樹脂で充填した。冷却ファンより送風を行い成形品を冷却した後、型開きして成形品を取り出した。不要な端部を切断し、図5に示すようなリブ(7)を有する平板(8)を得た。得られたリブを有する平板は外観良好であった。
A molded product made of a thermoplastic resin was produced by a method shown in FIG. 1 using a polypropylene foam sheet (product name: Sumiceller Foam PP sheet manufactured by Sumika Plustech) having a foaming ratio of 3 times and a thickness of 3 mm.
Recessed portion (5) for forming ribs (as shown in FIG. 2, recessed portion opening thickness (9) 5 mm, anti-opening portion thickness (10) 4 mm, height (11) 5 mm, length (12) 370 mm) , Volume (13) 8325 mm 3 , recess opening area (14) 1850 mm 2 in shape) on the molding surface, and mold B (6) that can be shaped into a flat plate shape. Using a pair of molds, a flat plate having ribs was formed. The molding die A is provided with a resin passage (4) capable of supplying a molten thermoplastic resin so as to communicate with the concave portion, and is provided with a molten thermoplastic resin pressure measuring sensor in the vicinity of the concave portion of the resin passage. It was a type. Mold A (3) was used with its temperature adjusted to 60 ° C.
While the thermoplastic resin foam sheet (1) is fixed to the clamp frame (2) of a vacuum forming machine (VAIM0301 manufactured by Sato Tekko Co., Ltd.) equipped with an extruder, the upper surface of the sheet becomes 190 ° C. by a near infrared heater. Was softened by heating. The foam sheet (1) softened by heating was supplied between the mold A (3) and the mold B (6) in a state of being fixed by the clamp frame (2).
Next, the mold A (3) and the mold B (6) were closed, and formed into a flat thermoplastic resin molded product having a thickness of 2.8 mm by press molding.
Propylene-based resin (manufactured by Sumitomo Chemical Co., Ltd., Nobrene BUE81E6, MFR = 80 g / min) is supplied to the concave portion of the mold at 3 g / sec through the resin passage (4) in the mold A (3) for 2.5 seconds. The concave portion was filled with a molten thermoplastic resin. After cooling the molded product by blowing air from a cooling fan, the mold was opened and the molded product was taken out. Unnecessary end portions were cut to obtain a flat plate (8) having ribs (7) as shown in FIG. The obtained flat plate having ribs had good appearance.

[比較例1]
実施例1において、リブを形成するための凹部形状が異なる(凹部の開口部厚み2.5mm、反開口部厚み2mm、高さ15mm、長さ370mm、体積12488mm3、凹部の開口部面積925mm2 )成形型Aを使用し、成形型凹部に3g/secで3.8秒間溶融状熱可塑性樹脂を供給する以外は、実施例1と同様にしてリブを有する平板を製造した。
得られたリブを有する平板は、溶融状熱可塑性樹脂が熱可塑性樹脂製発泡シート内に潜り込み、反リブ面側に隆起状の外観不良が発生した。
[Comparative Example 1]
In Example 1, the shape of the recesses for forming the ribs is different (the recess opening thickness is 2.5 mm, the counter opening thickness is 2 mm, the height is 15 mm, the length is 370 mm, the volume is 12488 mm 3 , and the opening area of the recess is 925 mm 2. ) using the mold a, except that supplying 3.8 seconds molten thermoplastic resin with 3 g / sec into the mold recess, to produce a flat plate having a rib in the same manner as in example 1.
In the obtained flat plate having ribs, the molten thermoplastic resin entered the foamed sheet made of thermoplastic resin, and a raised appearance defect occurred on the side opposite to the rib surface.

Figure 2007203502
Figure 2007203502

本発明の熱可塑性樹脂製成形品の製造方法の一例の概略図Schematic of an example of the manufacturing method of the thermoplastic resin molded article of the present invention 実施例1の成形型Aの平面図Plan view of mold A of Example 1 実施例1の成形型の断面図(図2の金型凹部を(a)方向に切断したもの)Sectional drawing of the shaping | molding die of Example 1 (thing which cut | disconnected the metal mold | die recessed part of FIG. 2 in the (a) direction) リブを有する平板の平面図Plan view of flat plate with ribs 実施例1で得られるリブを有する平板の断面図(図4のリブ部を(b)方向に切断したもの)Sectional drawing of the flat plate which has the rib obtained in Example 1 (what cut | disconnected the rib part of FIG. 4 in the (b) direction)

符号の説明Explanation of symbols

1 熱可塑性樹脂製発泡シート
2 クランプ枠
3 成形型A
4 樹脂通路
5 凹部
6 成形型B
7 リブ
8 熱可塑性樹脂製成形品(平板)
9 成形型A凹部の開口部厚み
10 成形型A凹部の反開口部厚み
11 成形型A凹部の高さ
12 成形型A凹部の長さ
13 成形型A凹部の体積
DESCRIPTION OF SYMBOLS 1 Thermoplastic resin foam sheet 2 Clamp frame 3 Mold A
4 Resin passage 5 Recess 6 Mold D
7 Rib 8 Molded product made of thermoplastic resin (flat plate)
9 Mold Opening A Recess Thickness 10 Mold A Recessed Opening Thickness 11 Mold D Recess Height 12 Mold A Recess Length 13 Mold D Recess Volume

Claims (2)

熱可塑性樹脂製発泡シートの一部にリブが融着されてなる熱可塑性樹脂製成形品であって、該リブの形状が式(A)を満たす熱可塑性樹脂製成形品
1mm≦(V1/S1)≦9mm 式(A)
1:リブの体積(mm3
1:リブの融着部面積(mm2
A molded product made of a thermoplastic resin in which a rib is fused to a part of a foamed sheet made of a thermoplastic resin, and the molded product made of a thermoplastic resin satisfying the formula (A) 1 mm ≦ (V 1 / S 1 ) ≦ 9 mm Formula (A)
V 1 : rib volume (mm 3 )
S 1 : Rib fused area (mm 2 )
以下の工程を順に含む、熱可塑性樹脂製発泡シートの一部にリブが融着されてなる請求項1に記載の熱可塑性樹脂製成形品の製造方法。
(1)熱可塑性樹脂製発泡シートを加熱し軟化する工程
(2)前記リブを賦形するために、体積と開口部面積が式(B)を満たす凹部が成形面に形成された成形型Aと、該成形型Aと対を成す成形型Bとの間に、工程(1)で得られる熱可塑性樹脂製発泡シートを供給する工程
1mm≦(V2/S2)≦9mm 式(B)
2:凹部の体積(mm3
2:凹部の開口部面積(mm2
(3)成形型Aと成形型Bを型閉めし、熱可塑性樹脂製発泡シートを所定形状に賦形すると共に、成形型Aの成形面に形成された凹部の開口部を前記熱可塑性樹脂製発泡シートで塞ぐ工程
(4)該凹部に通ずるように成形型A内に設けられた樹脂通路を通じて溶融状熱可塑性樹脂を該凹部に供給し、該溶融状熱可塑性樹脂と前記熱可塑性樹脂製発泡シートとを融着一体化する工程
(5)溶融状熱可塑性樹脂の供給を停止すると同時または停止した後に、型開きして熱可塑性樹脂製成形品を取り出す工程
The method for producing a molded product of a thermoplastic resin according to claim 1, wherein the rib is fused to a part of the foamed sheet made of a thermoplastic resin, including the following steps in order.
(1) Step of heating and softening the foamed sheet made of thermoplastic resin (2) Mold A in which a concave portion whose volume and opening area satisfy the formula (B) is formed on the molding surface in order to shape the rib And a step of supplying the thermoplastic resin foam sheet obtained in the step (1) between the mold A and the mold B paired with the mold A 1 mm ≦ (V 2 / S 2 ) ≦ 9 mm Formula (B)
V 2 : Volume of the recess (mm 3 )
S 2 : Opening area of the recess (mm 2 )
(3) The mold A and the mold B are closed, the thermoplastic resin foam sheet is shaped into a predetermined shape, and the opening of the recess formed on the molding surface of the mold A is made of the thermoplastic resin. Step 4 of closing with foam sheet (4) A molten thermoplastic resin is supplied to the concave portion through a resin passage provided in the mold A so as to communicate with the concave portion, and the molten thermoplastic resin and the thermoplastic resin foam are supplied. Step of fusing and integrating the sheet (5) Step of simultaneously opening or stopping the supply of the molten thermoplastic resin and then opening the mold to take out the molded product made of the thermoplastic resin
JP2006022401A 2006-01-31 2006-01-31 Thermoplastic resin made molded product and its manufacturing method Pending JP2007203502A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5775828A (en) * 1980-10-30 1982-05-12 Fujitsu Kasei Kk Resin molded object
JP2003053776A (en) * 2001-08-15 2003-02-26 Sanwa Kako Kk Method for manufacturing laminated molded article
JP2003231195A (en) * 2002-02-12 2003-08-19 Sumitomo Chem Co Ltd Foamed thermoplastic resin molding having functional member
JP2007050558A (en) * 2005-08-16 2007-03-01 Kasai Kogyo Co Ltd Interior trimming part for car

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5775828A (en) * 1980-10-30 1982-05-12 Fujitsu Kasei Kk Resin molded object
JP2003053776A (en) * 2001-08-15 2003-02-26 Sanwa Kako Kk Method for manufacturing laminated molded article
JP2003231195A (en) * 2002-02-12 2003-08-19 Sumitomo Chem Co Ltd Foamed thermoplastic resin molding having functional member
JP2007050558A (en) * 2005-08-16 2007-03-01 Kasai Kogyo Co Ltd Interior trimming part for car

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