JP2015189815A - Polystyrene-based resin foam sheet and method for producing the same - Google Patents

Polystyrene-based resin foam sheet and method for producing the same Download PDF

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JP2015189815A
JP2015189815A JP2014066755A JP2014066755A JP2015189815A JP 2015189815 A JP2015189815 A JP 2015189815A JP 2014066755 A JP2014066755 A JP 2014066755A JP 2014066755 A JP2014066755 A JP 2014066755A JP 2015189815 A JP2015189815 A JP 2015189815A
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foamed
polystyrene
foam
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JP6212422B2 (en
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久和 中島
Hisakazu Nakajima
久和 中島
晋 荒川
Susumu Arakawa
晋 荒川
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SHONAN SEKISUI KOGYO KK
Sekisui Kasei Co Ltd
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SHONAN SEKISUI KOGYO KK
Sekisui Plastics Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a foam sheet having satisfactory appearance, excellent dimensional stability, and flexibility and having cushioning properties, and a method for producing the foam sheet.SOLUTION: There is provided a polystyrene-based resin foam sheet in which thickness is 1.0 to 10 mm, the ratio of the surface layer density d2 from the surface to a depth of 0.2 mm, to the total density d1 (d2/d1) is 0.8 to 1.8, and an open cell ratio is 9 to 30 vol.%. There is also provided a method for producing the polystyrene-based resin foam sheet including a process where a polystyrene-based resin foam sheet is heated with vapor so as to be foamed to obtain a polystyrene-based foam sheet, in which the polystyrene-based resin foam sheet has a thickness of 0.5 to 5.0 mm, and in which the ratio of the surface layer density d4 from the surface to a depth of 0.2 mm, to the total density d3 (d4/d3) is 1.0 to 1.8, and an open cell ratio is 5 to 26 vol.%.

Description

本発明は、ポリスチレン系樹脂発泡板およびその製造方法に関する。   The present invention relates to a polystyrene-based resin foam plate and a method for producing the same.

ポリスチレン系樹脂発泡板(以下、単に発泡板という。)は、緩衝材、模型飛行機等の玩具、POP用ディスプレイ基板等の様々な用途に広く用いられている。該発泡板は、ポリスチレン系樹脂と発泡剤を含む溶融混練物を一次発泡させたポリスチレン系樹脂発泡シート(以下、単に発泡シートという。)を二次発泡させることで得られる。   Polystyrene resin foam plates (hereinafter simply referred to as foam plates) are widely used in various applications such as cushioning materials, toys such as model airplanes, POP display substrates, and the like. The foamed plate can be obtained by secondarily foaming a polystyrene resin foam sheet (hereinafter simply referred to as a foam sheet) obtained by first foaming a melt-kneaded product containing a polystyrene resin and a foaming agent.

発泡板の具体例としては、例えば、以下のものが挙げられる。
(i)Tダイ法またはインフレーション法により得た厚み0.1〜5mmの発泡シートを上下から無端帯金網で挟んだ状態で水蒸気により加熱し、発泡させて得られる発泡板(特許文献1)。
(ii)押出発泡により得た発泡シートの表裏両面に水蒸気を接触させて加熱し、発泡させて得られる発泡板(特許文献2)。
Specific examples of the foam plate include the following.
(I) A foamed plate obtained by heating and foaming a foam sheet having a thickness of 0.1 to 5 mm obtained by a T-die method or an inflation method with water from above and below with an endless wire mesh (Patent Document 1).
(Ii) A foamed plate obtained by bringing water vapor into contact with both front and back surfaces of a foamed sheet obtained by extrusion foaming, heating and foaming (Patent Document 2).

発泡板(i)、(ii)では、表面形状にムラが生じ、外観不良となることがある。また、製造後に厚みが収縮したり、三次発泡が起きたりすることで、製造後の寸法が変化してしまうことがある。また、表面硬度が高くなりすぎて、柔軟性が不充分となり、緩衝性に劣ることがある。   In the foamed plates (i) and (ii), the surface shape may be uneven, resulting in poor appearance. Moreover, the dimension after manufacture may change because thickness shrinks after manufacture or tertiary foaming occurs. Further, the surface hardness becomes too high, the flexibility becomes insufficient, and the buffering property may be inferior.

ところで、熱成形用の原反としては、厚みが0.5〜5mm、見かけ密度が70〜150kg/m、連続気泡率が0〜15体積%とされた発泡シートが提案されている(特許文献3)。しかし、該発泡シートを発泡板の原反とし、蒸気発泡(二次発泡)させて発泡板とすると、コルゲーションが発生してフラットな発泡板とならず、外観不良となる。 By the way, as a raw material for thermoforming, a foam sheet having a thickness of 0.5 to 5 mm, an apparent density of 70 to 150 kg / m 3 , and an open cell ratio of 0 to 15% by volume has been proposed (patent) Reference 3). However, when the foamed sheet is used as the raw material of the foamed plate and is foamed by steam foaming (secondary foaming), corrugation occurs and the flat foamed plate is not formed, resulting in poor appearance.

特公昭45−29394号公報Japanese Examined Patent Publication No. 45-29394 特開昭63−122515号公報JP 63-122515 A 特開2007−217711号公報JP 2007-217711 A

本発明は、外観が良好で、寸法安定性に優れ、かつ柔軟性があり、緩衝性を有する発泡板、および該発泡板の製造方法を提供することを目的とする。   An object of the present invention is to provide a foamed plate having a good appearance, excellent dimensional stability, flexibility, and buffering properties, and a method for producing the foamed plate.

本発明の発泡板は、厚みが1.0〜10mmであり、全体密度d1に対する、表面から深さ0.2mmまでの表層密度d2の比(d2/d1)が0.8〜1.8であり、連続気泡率が9〜30体積%であることを特徴とする。   The foamed plate of the present invention has a thickness of 1.0 to 10 mm, and the ratio (d2 / d1) of the surface layer density d2 from the surface to the depth of 0.2 mm with respect to the total density d1 is 0.8 to 1.8. Yes, the open cell rate is 9 to 30% by volume.

本発明の発泡板では、JIS K7171−2008に準拠して3点押し曲げ試験を行ったときの弾性率が10〜30MPaであることが好ましい。   The foamed plate of the present invention preferably has an elastic modulus of 10 to 30 MPa when a three-point press bending test is performed in accordance with JIS K7171-2008.

本発明の発泡板の製造方法は、前記した本発明の発泡板を製造する方法であって、発泡シートを蒸気で加熱して発泡させ、発泡板を得る工程を有し、前記発泡シートは、厚みが0.5〜5.0mmであり、全体密度d3に対する、表面から深さ0.2mmまでの表層密度d4の比(d4/d3)が1.0〜1.8であり、連続気泡率が5〜26体積%であることを特徴とする。   The method for producing a foamed plate according to the present invention is a method for producing the foamed plate according to the present invention, and includes a step of heating the foamed sheet with steam to obtain a foamed plate, The thickness is 0.5 to 5.0 mm, the ratio (d4 / d3) of the surface layer density d4 from the surface to the depth of 0.2 mm to the total density d3 is 1.0 to 1.8, and the open cell ratio Is 5 to 26% by volume.

本発明の発泡板の製造方法では、前記蒸気が水蒸気であることが好ましい。   In the manufacturing method of the foam board of this invention, it is preferable that the said steam is water vapor | steam.

本発明の発泡板は、外観が良好で、寸法安定性に優れ、かつ柔軟性があり、緩衝性を有する。
また、本発明の発泡板の製造方法によれば、外観が良好で、寸法安定性に優れ、かつ柔軟性があり、緩衝性を有する発泡板が得られる。
The foamed board of the present invention has a good appearance, excellent dimensional stability, flexibility, and buffering properties.
Moreover, according to the method for producing a foamed plate of the present invention, a foamed plate having good appearance, excellent dimensional stability, flexibility, and buffering properties can be obtained.

本発明の発泡板の製造方法の一例を示した模式図である。It is the schematic diagram which showed an example of the manufacturing method of the foamed board of this invention. 本発明の発泡板の製造方法の他の例を示した模式図である。It is the schematic diagram which showed the other example of the manufacturing method of the foam board of this invention.

本明細書において、発泡板の「表層」とは、発泡板の表面から深さ0.2mmまでの層を意味する。同様に、発泡シートの「表層」とは、発泡シートの表面から深さ0.2mmまでの層を意味する。   In this specification, the “surface layer” of the foam plate means a layer having a depth of 0.2 mm from the surface of the foam plate. Similarly, the “surface layer” of the foam sheet means a layer having a depth of 0.2 mm from the surface of the foam sheet.

<発泡板>
本発明の発泡板は、ポリスチレン系樹脂を含有する板状の発泡体、いわゆるポリスチレンペーパー(PSP)である。
本発明の発泡板は、厚みが1.0〜10mmであり、全体密度d1に対する、表面から深さ0.2mmまでの表層密度d2の比(d2/d1)が0.8〜1.8であり、連続気泡率が9〜30体積%である。ただし、表層密度d2は、発泡板の両面のそれぞれの表層密度の平均値とする。
厚み、比(d2/d1)および連続気泡率を前記範囲に制御することで、表面形状にムラが生じることが抑制され、フラットで良好な外観を有し、かつ製造後に収縮や三次発泡が起きにくく優れた寸法安定性を有する発泡板となる。また、表面硬度が高くなりすぎず、柔軟性があり、緩衝性を有する発泡板となる。
<Foam board>
The foamed plate of the present invention is a plate-like foam containing a polystyrene resin, so-called polystyrene paper (PSP).
The foamed plate of the present invention has a thickness of 1.0 to 10 mm, and the ratio (d2 / d1) of the surface layer density d2 from the surface to the depth of 0.2 mm with respect to the total density d1 is 0.8 to 1.8. Yes, the open cell ratio is 9 to 30% by volume. However, the surface layer density d2 is an average value of the surface layer densities of both surfaces of the foamed plate.
By controlling the thickness, the ratio (d2 / d1) and the open cell ratio within the above ranges, unevenness in the surface shape is suppressed, a flat and good appearance is obtained, and shrinkage and tertiary foaming occur after production. It becomes difficult to obtain a foamed plate having excellent dimensional stability. Further, the surface hardness is not excessively high, and the foamed plate has flexibility and cushioning properties.

発泡体の厚みは、1.0〜10mmであり、1.0〜8.0mmが好ましく、1.0〜7.0mmがより好ましい。発泡体の厚みが前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板となる。発泡体の厚みが前記上限値以下であれば、柔軟性があり、また軽量化が容易になる。   The thickness of the foam is 1.0 to 10 mm, preferably 1.0 to 8.0 mm, and more preferably 1.0 to 7.0 mm. If the thickness of the foam is equal to or greater than the lower limit value, the foam has a good appearance and has excellent dimensional stability. If the thickness of the foam is not more than the above upper limit value, there is flexibility and weight reduction is facilitated.

発泡板の全体密度d1に対する表層密度d2の比(d2/d1)は、0.8〜1.8であり、0.8〜1.7が好ましく、0.8〜1.6がより好ましい。比(d2/d1)が前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板となる。比(d2/d1)が前記上限値以下であれば、柔軟性がある発泡板となる。   The ratio (d2 / d1) of the surface layer density d2 to the overall density d1 of the foamed plate is 0.8 to 1.8, preferably 0.8 to 1.7, and more preferably 0.8 to 1.6. If ratio (d2 / d1) is more than the said lower limit, it will become a foam board with the favorable external appearance and the outstanding dimensional stability. If ratio (d2 / d1) is below the said upper limit, it will become a flexible foam board.

発泡板の全体密度d1は、0.03〜0.15g/cmが好ましく、0.035〜0.09g/cmがより好ましく、0.04〜0.08g/cmがさらに好ましい。全体密度d1が前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板となりやすい。全体密度d1が前記上限値以下であれば、柔軟性がある発泡板となりやすい。 Overall density d1 of the foam plate is preferably 0.03~0.15g / cm 3, more preferably 0.035~0.09g / cm 3, more preferably 0.04~0.08g / cm 3. If the overall density d1 is equal to or more than the lower limit value, it is easy to obtain a foamed plate having good appearance and excellent dimensional stability. If the overall density d1 is equal to or less than the upper limit value, a flexible foam plate is likely to be obtained.

発泡板の表層密度d2は、0.03〜0.15g/cmが好ましく、0.035〜0.12g/cmがより好ましく、0.04〜0.10g/cmがさらに好ましい。表層密度d2が前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板となりやすい。表層密度d2が前記上限値以下であれば、柔軟性がある発泡板となりやすい。 Surface density d2 of the foam plate is preferably 0.03~0.15g / cm 3, more preferably 0.035~0.12g / cm 3, more preferably 0.04~0.10g / cm 3. When the surface layer density d2 is equal to or higher than the lower limit value, it is easy to obtain a foamed plate having a good appearance and excellent dimensional stability. If surface layer density d2 is below the said upper limit, it will become a flexible foam board easily.

発泡板の連続気泡率は、9〜30体積%であり、10〜28体積%が好ましく、10〜25体積%がより好ましい。発泡体の連続気泡率が前記下限値以上であれば、柔軟性があり、緩衝性を有する発泡板となる。発泡体の連続気泡率が前記範囲内であれば、外観が良好で、優れた寸法安定性を有する発泡板となる。   The open cell ratio of the foamed plate is 9 to 30% by volume, preferably 10 to 28% by volume, and more preferably 10 to 25% by volume. When the open cell ratio of the foam is not less than the lower limit, the foamed plate is flexible and has a buffering property. When the open cell ratio of the foam is within the above range, the foam has a good appearance and has excellent dimensional stability.

発泡板の表面硬度は、50〜75が好ましく、53〜73がより好ましい。発泡板の表面硬度が前記下限値以上であれば、優れた寸法安定性が得られやすい。発泡板の表面硬度が前記上限値以下であれば、柔軟性があり、優れた緩衝性を有する発泡板となりやすい。   50-75 are preferable and, as for the surface hardness of a foamed board, 53-73 are more preferable. If the surface hardness of the foamed plate is equal to or higher than the lower limit, excellent dimensional stability is easily obtained. If the surface hardness of the foamed plate is not more than the above upper limit value, the foamed plate is flexible and easily has a good cushioning property.

発泡板の坪量は、75〜400g/mが好ましく、100〜350g/mがより好ましい。発泡板の坪量が前記下限値以上であれば、発泡板の強度を保ちやすい。発泡板の坪量が前記上限値以下であれば、柔軟性があり、緩衝性を有する発泡板となりやすい。 The basis weight of the foam plate is preferably 75~400g / m 2, 100~350g / m 2 is more preferable. If the basis weight of the foamed plate is equal to or greater than the lower limit value, it is easy to maintain the strength of the foamed plate. If the basis weight of the foamed plate is equal to or less than the above upper limit value, the foamed plate is flexible and easily has a cushioning property.

発泡板の最大点応力は、100〜650kPaが好ましく、150〜600kPaがより好ましい。発泡板の最大点応力が前記下限値以上であれば、発泡板の強度を保ちやすい。発泡板の最大点応力が前記上限値以下であれば、柔軟性があり、緩衝性を有する発泡板となりやすい。
なお、最大点応力とは、JIS K7171−2008に準拠して3点押し曲げ試験を行ったときの最大点応力を意味する。
100-650 kPa is preferable and, as for the maximum point stress of a foamed board, 150-600 kPa is more preferable. If the maximum point stress of the foamed plate is equal to or greater than the lower limit, the strength of the foamed plate is easily maintained. If the maximum point stress of the foamed plate is equal to or less than the upper limit, the foamed plate is flexible and easily has a buffering property.
The maximum point stress means the maximum point stress when a three-point press bending test is performed in accordance with JIS K7171-2008.

発泡板の弾性率は、10〜30MPaが好ましく、12〜25MPaがより好ましい。発泡板の弾性率が前記下限値以上であれば、発泡板の強度を保ちやすい。発泡板の弾性率が前記上限値以下であれば、柔軟性があり、緩衝性を有する発泡板となりやすい。
なお、弾性率とは、JIS K7171−2008に準拠して3点押し曲げ試験を行ったときの弾性率を意味する。
The elastic modulus of the foamed plate is preferably 10 to 30 MPa, and more preferably 12 to 25 MPa. If the elastic modulus of the foamed plate is equal to or higher than the lower limit, the strength of the foamed plate is easily maintained. If the elastic modulus of the foamed plate is not more than the above upper limit value, the foamed plate is flexible and easily has a buffering property.
The elastic modulus means an elastic modulus when a three-point press bending test is performed in accordance with JIS K7171-2008.

ポリスチレン系樹脂としては、特に限定されず、例えば、スチレン系単量体の単独重合体または共重合体等が挙げられる。また、ポリスチレン系樹脂としては、スチレン系単量体と、該スチレン系単量体と共重合可能なビニル系単量体とを共重合させた、スチレン系単量体を主成分とする共重合体を用いてもよい。
ポリスチレン系樹脂としては、スチレンに基づく構成単位を全構成単位に対して50質量%以上有するポリスチレン系樹脂が好ましく、ポリスチレンがより好ましい。
The polystyrene resin is not particularly limited, and examples thereof include homopolymers or copolymers of styrene monomers. In addition, the polystyrene resin includes a copolymer having a styrene monomer as a main component, which is a copolymer of a styrene monomer and a vinyl monomer copolymerizable with the styrene monomer. A coalescence may be used.
As the polystyrene-based resin, a polystyrene-based resin having 50% by mass or more of structural units based on styrene with respect to all the structural units is preferable, and polystyrene is more preferable.

スチレン系単量体としては、例えば、スチレン、α−メチルスチレン、ビニルトルエン、クロロスチレン、エチルスチレン、i−プロピルスチレン、ジメチルスチレン、ブロモスチレン等が挙げられる。
スチレン系単量体は、1種を単独で使用してもよく、2種以上を併用してもよい。
Examples of the styrene monomer include styrene, α-methyl styrene, vinyl toluene, chlorostyrene, ethyl styrene, i-propyl styrene, dimethyl styrene, bromostyrene, and the like.
A styrene-type monomer may be used individually by 1 type, and may use 2 or more types together.

スチレン系単量体と共重合可能なビニル系単量体としては、例えば、メチル(メタ)アクリレート、エチル(メタ)アクリレート、ブチル(メタ)アクリレート、セチル(メタ)アクリレート等のアルキル(メタ)アクリレート;(メタ)アクリロニトリル、ジメチルマレエート、ジメチルフマレート、ジエチルフマレート、エチルフマレート、ジビニルベンゼン、アルキレングリコールジメタクリレート等の二官能性単量体;等が挙げられる。
ビニル系単量体は、1種を単独で使用してもよく、2種以上を併用してもよい。
Examples of vinyl monomers copolymerizable with styrene monomers include alkyl (meth) acrylates such as methyl (meth) acrylate, ethyl (meth) acrylate, butyl (meth) acrylate, and cetyl (meth) acrylate. Bifunctional monomers such as (meth) acrylonitrile, dimethyl maleate, dimethyl fumarate, diethyl fumarate, ethyl fumarate, divinyl benzene, alkylene glycol dimethacrylate, and the like.
A vinyl-type monomer may be used individually by 1 type, and may use 2 or more types together.

原料となるポリスチレン系樹脂としては、市販のポリスチレン系樹脂、懸濁重合法等の方法で製造したポリスチレン系樹脂、リサイクル原料でないポリスチレン系樹脂(バージンポリスチレン)を使用できる他、使用済みの発泡板、ポリスチレン系樹脂発泡成形体(食品包装用トレー等)等を再生処理して得られたリサイクル原料を使用することができる。該リサイクル原料としては、使用済みの発泡板、ポリスチレン系樹脂発泡成形体を回収し、リモネン溶解方式や加熱減容方式によって再生したリサイクル原料を用いることができる。
ポリスチレン系樹脂は、1種を単独で使用してもよく、2種以上を併用してもよい。
The polystyrene resin used as a raw material can be a commercially available polystyrene resin, a polystyrene resin produced by a method such as suspension polymerization, a polystyrene resin that is not a recycled material (virgin polystyrene), a used foamed plate, Recycled raw materials obtained by reclaiming polystyrene-based resin foam molded articles (such as food packaging trays) can be used. As the recycled material, it is possible to use a recycled material obtained by recovering a used foamed plate or polystyrene-based resin foam-molded product and regenerating it by a limonene dissolution method or a heating volume reduction method.
Polystyrene resins may be used alone or in combination of two or more.

本発明の発泡体においては、ポリスチレン系樹脂が主成分である範囲で、ポリスチレン系樹脂に他の樹脂を配合してもよい。ポリスチレン系樹脂が主成分であるとは、発泡体の全樹脂成分(100質量%)に対するポリスチレン系樹脂の割合が50質量%以上であることを意味する。   In the foam of this invention, you may mix | blend another resin with a polystyrene resin in the range which has a polystyrene resin as a main component. That the polystyrene resin is a main component means that the ratio of the polystyrene resin to the total resin component (100% by mass) of the foam is 50% by mass or more.

他の樹脂を配合したポリスチレン系樹脂としては、例えば、発泡板の耐衝撃性を向上させるものとして、ジエン系のゴム状重合体(ポリブタジエン、スチレン−ブタジエン共重合体、エチレン−プロピレン−非共役ジエン三次元共重合体等)を配合したゴム変性ポリスチレン系樹脂、いわゆるハイインパクトポリスチレンが挙げられる。
また、他の樹脂としては、ポリエチレン系樹脂、ポリプロピレン系樹脂、アクリル系樹脂、アクリロニトリル−スチレン共重合体、アクリロニトリル−ブタジエン−スチレン共重合体等が挙げられる。
Examples of polystyrene resins blended with other resins include diene rubber polymers (polybutadiene, styrene-butadiene copolymer, ethylene-propylene-nonconjugated diene) for improving the impact resistance of foamed plates. Examples thereof include rubber-modified polystyrene resins blended with a three-dimensional copolymer or the like), so-called high impact polystyrene.
Examples of other resins include polyethylene resins, polypropylene resins, acrylic resins, acrylonitrile-styrene copolymers, acrylonitrile-butadiene-styrene copolymers, and the like.

また、他の樹脂としては、ポリフェニレンエーテル系樹脂を用いてもよい。ポリスチレン系樹脂にポリフェニレンエーテル系樹脂を配合することで、ポリスチレン系樹脂を単独で用いる場合に比べて、より靱性に優れ、割れにくく、強度に優れ、さらに耐熱性にも優れた発泡板となる。
ポリスチレン系樹脂にポリフェニレンエーテル系樹脂を配合する場合、ポリフェニレンエーテル系樹脂の割合は、全樹脂成分(100質量%)に対して、5質量%以上50質量%未満が好ましく、10〜40質量%がより好ましい。
他の樹脂は、1種を単独で使用してもよく、2種以上を併用してもよい。
Further, as other resins, polyphenylene ether resins may be used. By blending a polyphenylene ether-based resin with a polystyrene-based resin, the foamed plate is superior in toughness, hard to break, excellent in strength, and also excellent in heat resistance, compared to the case where the polystyrene-based resin is used alone.
When blending a polyphenylene ether resin with a polystyrene resin, the ratio of the polyphenylene ether resin is preferably 5% by mass or more and less than 50% by mass, and 10 to 40% by mass with respect to the total resin component (100% by mass). More preferred.
Another resin may be used individually by 1 type, and may use 2 or more types together.

本発明の発泡板には、物性を損なわない範囲内で、造核剤、架橋剤、充填剤、難燃剤、難燃助剤、滑剤(炭化水素、脂肪酸系、脂肪酸アミド系、エステル系、アルコール系、金属石鹸、シリコーン油、低分子ポリエチレン等のワックス等)、展着剤(流動パラフィン、ポリエチレングリコール、ポリブテン等)、着色剤等の添加剤を添加してもよい。なかでも、本発明の発泡板は、造核剤を含有することが好ましい。   The foamed plate of the present invention has a nucleating agent, a crosslinking agent, a filler, a flame retardant, a flame retardant aid, a lubricant (hydrocarbon, fatty acid, fatty acid amide, ester, alcohol within the range not impairing the physical properties. System, metal soap, silicone oil, wax such as low molecular weight polyethylene, etc.), spreading agents (liquid paraffin, polyethylene glycol, polybutene, etc.), colorants and other additives may be added. Especially, it is preferable that the foamed board of this invention contains a nucleating agent.

造核剤としては、例えば、タルク、炭酸水素ナトリウム、炭酸水素アンモニウム、炭酸カルシウム、クレー、クエン酸等が挙げられる。なかでも、造核剤としては、タルクが好ましい。造核剤は、1種を単独で使用してもよく、2種以上を併用してもよい。
造核剤の添加量は、ポリスチレン系樹脂100質量部に対して0.01〜5質量部が好ましい。
Examples of the nucleating agent include talc, sodium hydrogen carbonate, ammonium hydrogen carbonate, calcium carbonate, clay, citric acid and the like. Of these, talc is preferable as the nucleating agent. A nucleating agent may be used individually by 1 type, and may use 2 or more types together.
The addition amount of the nucleating agent is preferably 0.01 to 5 parts by mass with respect to 100 parts by mass of the polystyrene resin.

本発明の発泡板の少なくとも一方の表面には、紙または樹脂フイルムを積層することができる。発泡板の表面に紙や樹脂フイルムを積層することにより、表面をより美麗にし、また剛性をより高くすることができる。
樹脂フィルムは、着色料(顔料、染料等)を添加することで様々な色調に着色でき、また表面に印刷を施すことで様々な模様やデザインを表示できる。同様に、紙の表面に印刷を施すことで様々な模様やデザインを表示できる。
発泡板の表面に紙または樹脂フイルムを積層したものは、例えば、POP用ディスプレイ基板に使用できる。
Paper or a resin film can be laminated on at least one surface of the foamed plate of the present invention. By laminating paper or a resin film on the surface of the foamed plate, the surface can be made more beautiful and the rigidity can be made higher.
The resin film can be colored in various colors by adding colorants (pigments, dyes, etc.), and various patterns and designs can be displayed by printing on the surface. Similarly, various patterns and designs can be displayed by printing on the paper surface.
What laminated | stacked paper or the resin film on the surface of the foamed board can be used for the display substrate for POP, for example.

発泡板に積層する樹脂フィルムの材質としては、特に限定されず、例えば、ポリスチレン系樹脂、耐衝撃性ポリスチレン系樹脂、ポリエチレン系樹脂、ポリプロピレン系樹脂、アクリル酸系樹脂、ポリ乳酸系樹脂等の熱可塑性樹脂が挙げられる。   The material of the resin film laminated on the foam plate is not particularly limited. For example, heat such as polystyrene resin, impact-resistant polystyrene resin, polyethylene resin, polypropylene resin, acrylic resin, polylactic acid resin, etc. A plastic resin is mentioned.

発泡板に積層する紙または樹脂フィルムの厚みは、10〜100μmが好ましい。
紙の積層方法としては、ホットメルト系接着剤等の接着剤により積層する方法等が挙げられる。
樹脂フィルムの積層方法としては、溶融状態とした熱可塑性樹脂を発泡板の表面にフィルム状に押出して熱融着させる方法、樹脂フィルムを発泡板に重ね合わせ、熱融着または接着剤により接着する方法等が挙げられる。
As for the thickness of the paper or resin film laminated | stacked on a foamed board, 10-100 micrometers is preferable.
Examples of the paper lamination method include a method of laminating with an adhesive such as a hot melt adhesive.
As a method of laminating the resin film, a thermoplastic resin in a molten state is extruded into a film shape on the surface of the foamed plate and thermally fused, or the resin film is superimposed on the foamed plate and adhered by thermal fusion or an adhesive. Methods and the like.

以上説明した本発明の発泡板は、厚み、全体密度d1に対する表層密度d2の比(d2/d1)、および連続気泡率が特定の範囲に制御されているため、外観が良好で、製造後に寸法が変化しにくく寸法安定性に優れるうえ、柔軟性があり、優れた緩衝性を有する。   The foamed plate of the present invention described above has a good appearance and is dimensioned after production because the thickness, the ratio of the surface layer density d2 to the overall density d1 (d2 / d1), and the open cell ratio are controlled within a specific range. Is difficult to change, has excellent dimensional stability, is flexible, and has excellent buffering properties.

<発泡板の製造方法>
本発明の発泡板の製造方法としては、例えば、下記の一次発泡工程および二次発泡工程を有する方法が挙げられる。
一次発泡工程:少なくともポリスチレン系樹脂と発泡剤を溶融混練した溶融混練物を押出機から押出して発泡(一次発泡)させ、発泡シート(一次シート)を得る工程。
二次発泡工程:発泡シートを蒸気により加熱して発泡(二次発泡)させ、発泡板を得る工程。
<Method for producing foam plate>
As a manufacturing method of the foam board of this invention, the method of having the following primary foaming process and secondary foaming process is mentioned, for example.
Primary foaming step: a step of obtaining a foamed sheet (primary sheet) by extruding a melt-kneaded material obtained by melt-kneading at least a polystyrene resin and a foaming agent from an extruder and foaming (primary foaming).
Secondary foaming step: a step of heating a foamed sheet with steam to foam (secondary foaming) to obtain a foamed plate.

[一次発泡工程]
一次発泡工程では、例えば、ポリスチレン系樹脂、および必要に応じて用いる他の樹脂、造核剤等を押出機に供給して加熱溶融し、発泡剤を加えて混練し、押出機の先端に取り付けられた金型から押出しつつ発泡(一次発泡)させ、得られた発泡シート(一次シート)を巻き取って回収する。回収した発泡シートは、発泡板の原反となる。
[Primary foaming process]
In the primary foaming process, for example, polystyrene resin, and other resins used as necessary, nucleating agent, etc. are supplied to the extruder, melted by heating, added with the foaming agent, kneaded, and attached to the tip of the extruder Foaming (primary foaming) is performed while extruding from the obtained mold, and the obtained foamed sheet (primary sheet) is wound up and collected. The recovered foam sheet becomes a raw sheet of the foam plate.

発泡剤としては、物理発泡剤が好ましい。
物理発泡剤としては、炭素数6以下の炭化水素(例えばプロパン、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、ネオペンタン、シクロペンタン等の脂肪族炭化水素)が好ましく、ノルマルブタン、イソブタン、ノルマルペンタン、イソペンタンがより好ましい。発泡剤は、1種を単独で使用してもよく、2種以上を併用してもよい。
発泡剤の使用量は、使用する全樹脂成分100質量部に対して、1.0〜6.0質量部が好ましく、1.5〜5.0質量部がより好ましい。
As the foaming agent, a physical foaming agent is preferable.
As the physical foaming agent, hydrocarbons having 6 or less carbon atoms (for example, aliphatic hydrocarbons such as propane, normal butane, isobutane, normal pentane, isopentane, neopentane, and cyclopentane) are preferable, and normal butane, isobutane, normal pentane, and isopentane. Is more preferable. A foaming agent may be used individually by 1 type, and may use 2 or more types together.
1.0-6.0 mass parts is preferable with respect to 100 mass parts of all the resin components to be used, and 1.5-5.0 mass parts is more preferable.

押出機の先端に取り付ける金型としては、例えば、環状開口を有する環状金型(サーキュラーダイ)、Tダイ等が挙げられる。
環状金型を用いる場合の具体的な態様としては、例えば、環状金型から押出した円筒状発泡体を冷却マンドレルに沿わせつつ、該円筒状発泡体の外面に冷却エアーを吹き付けて冷却し、該冷却マンドレルの先端部の両側に設けたカッターにより、該円筒状発泡体に軸方向に切れ目を入れて切開し、2枚の発泡シートとする態様が挙げられる。
As a metal mold | die attached to the front-end | tip of an extruder, the cyclic | annular metal mold | die (circular die) which has cyclic | annular opening, T-die, etc. are mentioned, for example.
As a specific aspect in the case of using the annular mold, for example, while cooling the cylindrical foam extruded from the annular mold along the cooling mandrel, cooling is performed by blowing cooling air to the outer surface of the cylindrical foam, A mode in which the cylindrical foam is cut in an axial direction with a cutter provided on both sides of the front end portion of the cooling mandrel is cut into two foam sheets.

一次発泡における発泡倍率は、7〜15倍が好ましく、9〜12倍がより好ましい。一次発泡における発泡倍率が前記下限値以上であれば、発泡板の軽量化が容易になる。一次発泡における発泡倍率が前記上限値以下であれば、強度の高い発泡板が得られやすい。   The expansion ratio in primary foaming is preferably 7 to 15 times, and more preferably 9 to 12 times. If the expansion ratio in primary foaming is equal to or greater than the lower limit, the foamed plate can be easily reduced in weight. If the expansion ratio in primary foaming is less than or equal to the above upper limit value, it is easy to obtain a foam plate having high strength.

一次発泡工程では、得られる発泡シートが後述の厚み、全体密度d3に対する、表面から深さ0.2mmまでの表層密度d4の比(d4/d3)、および連続気泡率の各条件を満たすように製造条件を制御することが好ましい。
例えば、発泡剤の量を調節することで、発泡シートの厚みを制御できる。また金型の温度をより高くすることで、発泡シートの比(d4/d3)をより小さくすることができる。また、ポリスチレン系樹脂を溶融した後の温度を高くすることより、発泡シートの連続気泡率を高くすることができる。
In the primary foaming step, the obtained foamed sheet satisfies the following conditions: thickness, overall density d3, ratio of surface layer density d4 from the surface to a depth of 0.2 mm (d4 / d3), and open cell ratio It is preferable to control the production conditions.
For example, the thickness of the foam sheet can be controlled by adjusting the amount of the foaming agent. Moreover, the ratio (d4 / d3) of a foam sheet can be made smaller by making the temperature of a metal mold | die higher. Moreover, the open cell ratio of a foamed sheet can be made high by raising the temperature after melting a polystyrene-type resin.

[二次発泡工程]
二次発泡工程では、例えば、図1に示すように、一次発泡工程で得られた発泡シートロール10から発泡シート1を送り出し、ガイドロール12によって蒸気発泡槽14内を通過するように連続的に搬送し、蒸気発泡槽14内で蒸気により加熱して発泡(二次発泡)させる。次いで、二次発泡させて得た発泡板2を冷却ロール16により冷却し、裁断機18により所定の寸法に裁断する。
発泡シートを蒸気により加熱して二次発泡させる方法は、発泡倍率を高くしやすく低密度な発泡板が得られやすい点、より柔軟性に優れ、優れた緩衝性を有する発泡板が得られる点で有利である。本発明では、ポリスチレン系樹脂との相性が良く、発泡シートを充分に二次発泡させやすい点から、蒸気として水蒸気を用いることが特に好ましい。
[Secondary foaming process]
In the secondary foaming process, for example, as shown in FIG. 1, the foamed sheet 1 is sent out from the foamed sheet roll 10 obtained in the primary foaming process and continuously passed through the steam foaming tank 14 by the guide roll 12. It is conveyed and heated by steam in the steam foaming tank 14 to be foamed (secondary foaming). Next, the foamed plate 2 obtained by secondary foaming is cooled by a cooling roll 16 and cut into a predetermined size by a cutting machine 18.
The method of secondary foaming by heating the foamed sheet with steam is easy to increase the foaming ratio and easily obtain a low density foamed board, and more flexible and excellent cushioning can be obtained. Is advantageous. In the present invention, it is particularly preferable to use water vapor as the vapor because the compatibility with the polystyrene resin is good and the foamed sheet can be sufficiently subjected to secondary foaming.

(発泡シート)
二次発泡工程に用いる発泡シートは、厚みが0.5〜5.0mmであり、全体密度d3に対する表層密度d4の比(d4/d3)が1.0〜1.8であり、連続気泡率が5〜26体積%であることが好ましい。
発泡シートを二次発泡させることでより厚みが増し、より密度が高くなり、より連続気泡率が増加した発泡板が得られる。
(Foam sheet)
The foam sheet used in the secondary foaming process has a thickness of 0.5 to 5.0 mm, a ratio of the surface layer density d4 to the total density d3 (d4 / d3) of 1.0 to 1.8, and an open cell ratio. Is preferably 5 to 26% by volume.
By subjecting the foamed sheet to secondary foaming, it is possible to obtain a foamed plate having an increased thickness, a higher density, and an increased open cell ratio.

発泡シートの連続気泡率を適度に高めることで発泡シート内に蒸気が均一に入りやすくなる。また、発泡シートの表層密度d4を全体密度d3に近づける、すなわち比(d4/d3)を1.0に近づけることで、発泡シート内に蒸気が均一に入りやすくなる。そのため、発泡シートが前記の条件を満たすことで該発泡シートを充分な発泡倍率で二次発泡させやすくなり、前述した厚み、比(d2/d1)および連続気泡率の各条件を満たす、外観が良好で優れた寸法安定性を有する発泡板を得ることが容易になる。
また、発泡シートが前記の条件を満たしていれば、より優れた柔軟性を有し、優れた緩衝性を有する発泡板が得られる。
By appropriately increasing the open cell ratio of the foam sheet, it becomes easy for vapor to easily enter the foam sheet. Further, by making the surface density d4 of the foamed sheet closer to the overall density d3, that is, by making the ratio (d4 / d3) closer to 1.0, it becomes easier for vapor to easily enter the foamed sheet. Therefore, when the foamed sheet satisfies the above-mentioned conditions, the foamed sheet can be easily subjected to secondary foaming at a sufficient foaming ratio, and the appearance satisfying the aforementioned conditions of thickness, ratio (d2 / d1) and open cell ratio It becomes easy to obtain a foamed plate having good and excellent dimensional stability.
Moreover, if the foamed sheet satisfies the above-mentioned conditions, a foamed plate having more excellent flexibility and excellent buffering properties can be obtained.

発泡シートの厚みは、0.5〜5.0mmが好ましく、0.9〜4.0mmがより好ましく、1.0〜3.7mmがさらに好ましい。発泡シートの厚みが前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板が得られやすい。発泡シートの厚みが前記上限値以下であれば、より柔軟性に優れ、優れた緩衝性を有する発泡板が得られやすく、また発泡板の軽量化が容易になる。   The thickness of the foamed sheet is preferably 0.5 to 5.0 mm, more preferably 0.9 to 4.0 mm, and further preferably 1.0 to 3.7 mm. If the thickness of the foamed sheet is equal to or more than the lower limit, a foamed plate having a good appearance and excellent dimensional stability can be easily obtained. If the thickness of the foamed sheet is not more than the above upper limit value, it is easy to obtain a foamed plate having better flexibility and excellent buffering properties, and the foamed plate can be easily reduced in weight.

発泡シートの全体密度d3に対する表層密度d4の比(d4/d3)は、1.0〜1.8が好ましく、1.0〜1.7がより好ましく、1.0〜1.6がさらに好ましい。比(d4/d3)が前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板が得られやすい。比(d4/d3)が前記上限値以下であれば、蒸気が発泡シート内により均一に入り、充分な発泡倍率で二次発泡させやすくなる。また、より柔軟性に優れ、優れた緩衝性を有する発泡板が得られやすい。   The ratio (d4 / d3) of the surface layer density d4 to the overall density d3 of the foamed sheet is preferably 1.0 to 1.8, more preferably 1.0 to 1.7, and still more preferably 1.0 to 1.6. . If the ratio (d4 / d3) is equal to or greater than the lower limit, a foamed plate having a good appearance and excellent dimensional stability can be easily obtained. If the ratio (d4 / d3) is less than or equal to the above upper limit value, the vapor enters the foamed sheet more uniformly, and secondary foaming is facilitated at a sufficient foaming ratio. Moreover, it is easy to obtain the foam board which is excellent in a softness | flexibility and has the outstanding buffer property.

発泡シートの全体密度d3は、0.04〜0.20g/cmが好ましく、0.05〜0.18g/cmがより好ましく、0.05〜0.15g/cmがさらに好ましい。全体密度d3が前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板が得られやすい。全体密度d3が前記上限値以下であれば、蒸気が発泡シート内により均一に入り、充分な発泡倍率で二次発泡させやすくなる。また、より柔軟性に優れ、優れた緩衝性を有する発泡板が得られやすい。 The total density d3 of the foamed sheet is preferably 0.04 to 0.20 g / cm 3 , more preferably 0.05 to 0.18 g / cm 3 , and even more preferably 0.05 to 0.15 g / cm 3 . If the overall density d3 is equal to or greater than the lower limit, it is easy to obtain a foamed plate having good appearance and excellent dimensional stability. If the overall density d3 is less than or equal to the above upper limit value, the vapor enters the foamed sheet more uniformly, and secondary foaming is facilitated at a sufficient foaming ratio. Moreover, it is easy to obtain the foam board which is excellent in a softness | flexibility and has the outstanding buffer property.

発泡シートの表層密度d4は、0.04〜0.25g/cmが好ましく、0.05〜0.23g/cmがより好ましく、0.05〜0.20g/cmがさらに好ましい。表層密度d4が前記下限値以上であれば、外観が良好で、優れた寸法安定性を有する発泡板が得られやすい。表層密度d4が前記上限値以下であれば、蒸気が発泡シート内により均一に入り、充分な発泡倍率で二次発泡させやすくなる。また、より柔軟性に優れ、優れた緩衝性を有する発泡板が得られやすい。 The surface density d4 of the foamed sheet is preferably 0.04 to 0.25 g / cm 3 , more preferably 0.05 to 0.23 g / cm 3 , and even more preferably 0.05 to 0.20 g / cm 3 . When the surface layer density d4 is equal to or higher than the lower limit value, it is easy to obtain a foamed plate having good appearance and excellent dimensional stability. If the surface layer density d4 is less than or equal to the above upper limit value, the vapor enters the foamed sheet more uniformly, and secondary foaming is facilitated at a sufficient foaming ratio. Moreover, it is easy to obtain the foam board which is excellent in a softness | flexibility and has the outstanding buffer property.

発泡シートの連続気泡率は、5〜26体積%が好ましく、5〜23体積%がより好ましく、5〜20体積%がさらに好ましい。発泡シートの連続気泡率が前記下限値以上であれば、発泡シート内に蒸気が入りやすく、充分な発泡倍率で二次発泡した充分な厚みの発泡板を得ることが容易になる。また、より柔軟性に優れ、優れた緩衝性を有する発泡板が得られやすい。発泡シートの連続気泡率が前記上限値以下であれば、外観が良好で、優れた寸法安定性を有する発泡板が得られやすい。   The open cell ratio of the foamed sheet is preferably 5 to 26% by volume, more preferably 5 to 23% by volume, and still more preferably 5 to 20% by volume. If the open cell ratio of the foamed sheet is equal to or greater than the lower limit, it is easy for steam to enter the foamed sheet, and it becomes easy to obtain a foamed sheet having a sufficient thickness that is secondarily foamed at a sufficient foaming ratio. Moreover, it is easy to obtain the foam board which is excellent in a softness | flexibility and has the outstanding buffer property. If the open cell ratio of the foamed sheet is not more than the above upper limit value, it is easy to obtain a foamed plate with good appearance and excellent dimensional stability.

二次発泡工程では、一次発泡工程で得られた発泡シートを大気圧条件下に置いて熟成させた後に二次発泡に用いることが好ましい。一次発泡直後の発泡シートでは、形成された気泡内に存在する気体状の発泡剤の体積が冷却によって収縮するために、気泡内が減圧状態になり、二次発泡を起こしにくい。発泡シートを熟成することで、シート外部から気泡内に空気が侵入し、気泡内が大気圧状態となる。これにより、発泡シートを充分な発泡倍率で二次発泡させやすくなる。また、二次発泡後に発泡板の気泡が収縮しにくくなるため、発泡板の寸法安定性がより良好になる。   In the secondary foaming process, it is preferable to use the foamed sheet obtained in the primary foaming process for secondary foaming after aging under atmospheric pressure conditions. In the foam sheet immediately after the primary foaming, the volume of the gaseous foaming agent present in the formed bubbles contracts due to cooling, so that the inside of the bubbles is in a reduced pressure state and secondary foaming hardly occurs. By aging the foam sheet, air enters the bubbles from the outside of the sheet, and the bubbles are in an atmospheric pressure state. This facilitates secondary foaming of the foamed sheet at a sufficient foaming ratio. Moreover, since the bubbles of the foamed plate are less likely to shrink after secondary foaming, the dimensional stability of the foamed plate becomes better.

蒸気発泡槽内の温度は、80〜120℃が好ましく、90〜110℃がより好ましい。   80-120 degreeC is preferable and, as for the temperature in a steam foaming tank, 90-110 degreeC is more preferable.

以上説明した本発明の発泡板の製造方法では、厚み、全体密度d1に対する表層密度d2の比(d2/d1)、および連続気泡率が特定の範囲に制御した発泡板とするため、得られる発泡板は外観が良好で、寸法安定性に優れるうえ、優れた緩衝性を有する。   In the foam plate manufacturing method of the present invention described above, the foam is obtained because the foam plate has a thickness, a ratio of the surface layer density d2 to the total density d1 (d2 / d1), and an open cell ratio controlled within a specific range. The plate has a good appearance, excellent dimensional stability, and excellent buffering properties.

なお、本発明の発泡板の製造方法は、前記した製造方法には限定されない。
本発明の発泡板の製造方法では、二次発泡させた発泡板の表面に紙または樹脂フィルムを積層してもよい。
具体的には、例えば、以下のような方法としてもよい。図2に示すように、発泡シートロール10から発泡シート1を送り出し、ガイドロール12によって蒸気発泡槽14内を通過させつつ、蒸気により加熱して発泡(二次発泡)させる。その後、接着剤付きの紙3を一対の紙ロール20から送り出して発泡板2の両面にそれぞれ重ね、接着用熱ロール22により加熱接着して積層体4とし、冷却ロール16により冷却し、裁断機18により所定の寸法に裁断する。樹脂フィルムを積層する場合は、紙ロール20の代わりに、発泡板と同素材の樹脂フィルムを用いるか、あるいは接着剤付きの樹脂フィルムが巻き回された樹脂フィルムロールを用いることで、前記した紙の場合と同様の方法で積層が行える。
In addition, the manufacturing method of the foamed board of this invention is not limited to an above described manufacturing method.
In the method for producing a foamed plate of the present invention, paper or a resin film may be laminated on the surface of the foamed plate subjected to secondary foaming.
Specifically, for example, the following method may be used. As shown in FIG. 2, the foamed sheet 1 is sent out from the foamed sheet roll 10, and is heated and foamed (secondary foaming) by steam while passing through the steam foaming tank 14 by the guide roll 12. Thereafter, the paper 3 with an adhesive is fed out from a pair of paper rolls 20 and stacked on both surfaces of the foamed plate 2, heated and bonded by a hot roll 22 for bonding to form a laminate 4, cooled by a cooling roll 16, and a cutting machine. 18 is cut into a predetermined size. When laminating a resin film, instead of the paper roll 20, a resin film made of the same material as the foam plate is used, or a resin film roll around which a resin film with an adhesive is wound is used. Lamination can be performed in the same manner as in the above.

以下、実施例によって本発明を詳細に説明するが、本発明は以下の記載によっては限定されない。
[坪量の測定]
発泡シートの幅方向の両端20mmを除いた部分を、幅方向に等間隔に10cm×10cmに切り取り、各切片の質量(g)を0.001g単位まで測定した。各切片の質量(g)の平均値を1m当たりの質量に換算した値を、発泡シートの坪量(g/m)とした。発泡板の坪量についても同様に測定した。
EXAMPLES Hereinafter, although an Example demonstrates this invention in detail, this invention is not limited by the following description.
[Measurement of basis weight]
The portion excluding both ends 20 mm in the width direction of the foamed sheet was cut into 10 cm × 10 cm at equal intervals in the width direction, and the mass (g) of each slice was measured to 0.001 g unit. A value obtained by converting an average value of the mass (g) of each section into a mass per 1 m 2 was defined as a basis weight (g / m 2 ) of the foamed sheet. It measured similarly about the basic weight of a foamed board.

[厚みの測定]
発泡シートにおける、その幅方向の両方の縁から20mmの端部領域を除いた部分において、ダイヤルシックネスゲージSM−112(テクロック社製)を用いて、幅方向に等間隔に9点以上厚みを測定し、それらの相加平均を厚みとした。発泡板の厚みについても同様に測定した。
[Measurement of thickness]
Using a dial thickness gauge SM-112 (manufactured by Tecrock Co., Ltd.), measure the thickness of 9 or more points at equal intervals in the width direction at the portion of the foam sheet excluding the 20 mm end region from both edges in the width direction. And the arithmetic mean of those was made into thickness. The thickness of the foam plate was also measured in the same manner.

[連続気泡率の測定]
発泡シートの連続気泡率は、ASTM D−2856−87に準拠して1−1/2−1気圧法にて測定した。
具体的には、発泡シートを一辺25mmの平面正方形状に切断し、この切断片を厚み方向に複数枚重ね合わせ、厚みが約25mmの試験片を作製した。同じ要領で合計5個の試験片を作製し、空気比較式比重計(東京サイエンス社製、商品名「1000型」)を用いて、1−1/2−1気圧法により各試験片の連続気泡率を測定した。1−1/2−1気圧法により測定した試験片の体積Vと、ノギスで測定した寸法から算出した同じ試験片の体積Vから、下式(1)より各試験片の連続気泡率Z(体積%)を算出し、それらの相加平均値を発泡シートの連続気泡率とした。
Z=(V−V)/V×100 ・・・(1)
発泡板の連続気泡率についても同様に測定した。
[Measurement of open cell ratio]
The open cell ratio of the foamed sheet was measured by the 1-1 / 2-1 atmospheric pressure method in accordance with ASTM D-2856-87.
Specifically, the foam sheet was cut into a flat square shape with a side of 25 mm, and a plurality of the cut pieces were overlapped in the thickness direction to prepare a test piece having a thickness of about 25 mm. A total of 5 test pieces were prepared in the same manner, and each test piece was continuously measured by the 1-1 / 2-1 atmospheric pressure method using an air-comparing hydrometer (manufactured by Tokyo Science Co., Ltd., trade name “1000 type”). The bubble rate was measured. From the volume V 0 of the test piece calculated from the size measured with the caliper and the volume V 0 of the test piece measured by the 1-1 / 2 atm method, the open cell ratio Z of each test piece is obtained from the following equation (1). (Vol%) was calculated, and the arithmetic mean value thereof was defined as the open cell ratio of the foam sheet.
Z = (V 0 −V) / V 0 × 100 (1)
The open cell ratio of the foamed plate was measured in the same manner.

[全体密度の測定]
発泡シートにおける、その幅方向の両方の縁から20mmの端部領域を除いた部分から、10cm×10cmの矩形の切片を、シートの幅方向に等間隔に9個以上切り出し、各切片の質量W(g)を測定した。また、ダイヤルシックネスゲージSM−112(テクロック社製)を用いて各切片の厚みを測定し、各切片の体積V(mm)を算出した。下式(2)により各切片の密度d(g/cm)を算出して、各切片の密度dを相加平均した値を発泡シートの全体密度d3とした。
=W/V×10 ・・・(2)
発泡板の全体密度d1についても同様に測定した。
[Measurement of total density]
Nine or more 10 cm × 10 cm rectangular sections are cut out at equal intervals in the width direction of the sheet from the portion excluding the end area of 20 mm from both edges in the width direction of the foam sheet, and the mass W of each section A (g) was measured. Further, the thickness of each section was measured using a dial thickness gauge SM-112 (manufactured by Teclock Co.), and the volume VA (mm 3 ) of each section was calculated. The density d A (g / cm 3 ) of each section was calculated by the following formula (2), and the value obtained by arithmetically averaging the density d A of each section was defined as the overall density d3 of the foam sheet.
d A = W A / V A × 10 3 (2)
The total density d1 of the foamed plate was measured in the same manner.

[表層密度の測定]
スライサー(フォーチュナ社(ドイツ)製スプリッティングマシン、型式AB−320−D)にて、発泡シートの両面の表層(厚み0.2mm)を切り取り、さらに幅25mm、長さ150mmにカットして測定用試験片とした。全体密度の測定の場合と同様に該測定用試験片の質量W(g)と体積V(mm)を測定し、下式(3)より発泡シートの表層密度d4(g/cm)を算出した。
d4=W/V×10 ・・・(3)
ただし、測定用試験片は、成形後72時間以上経過した発泡シートから切り取り、23±2℃、50±5RH%、または27±2℃、65±5RH%の雰囲気条件に16時間以上放置したものを測定に使用した。
発泡板の表層密度d2についても同様に測定した。
[Measurement of surface layer density]
Using a slicer (Split machine manufactured by Fortuna (Germany), model AB-320-D), cut off the surface layer (thickness 0.2 mm) on both sides of the foamed sheet, and cut it into a width of 25 mm and a length of 150 mm for measurement test It was a piece. The mass W B (g) and the volume V B (mm 3 ) of the test specimen for measurement are measured in the same manner as in the case of measuring the total density, and the surface layer density d4 (g / cm 3 ) of the foamed sheet is obtained from the following formula (3). ) Was calculated.
d4 = W B / V B × 10 3 (3)
However, the test specimen for measurement was cut from a foam sheet that had passed 72 hours or more after molding, and was left for 16 hours or more in an atmosphere of 23 ± 2 ° C., 50 ± 5 RH%, or 27 ± 2 ° C., 65 ± 5 RH%. Was used for the measurement.
The surface layer density d2 of the foam plate was also measured in the same manner.

[表面硬度の測定]
各例で得られた発泡板の表面硬度を以下の方法で測定した。
発泡板から幅130cm×長さ50cmの試験片を切り出し、アスカー表面硬度測定器(型式:「CS型」、アスカー社製)を用いて、表面硬度測定器を試験片表面に押し付けた際の値を表面硬度として測定した。また、測定は試験片において幅方向に20cmごと、押出方向に15cmごとに行い、それらの算術平均を表面硬度とした
[Measurement of surface hardness]
The surface hardness of the foamed board obtained in each example was measured by the following method.
A value obtained when a test piece having a width of 130 cm and a length of 50 cm is cut out from the foamed plate and the surface hardness tester is pressed against the surface of the test piece using an Asker surface hardness tester (model: “CS type”, manufactured by Asker). Was measured as surface hardness. In addition, the measurement is performed every 20 cm in the width direction and every 15 cm in the extrusion direction in the test piece, and the arithmetic average thereof is defined as the surface hardness.

[外観評価]
得られた発泡板を目視で確認し、以下の基準で外観を評価した。
○(良好):凹凸ムラがなく、平滑性がある。
×(不良):凹凸ムラがあり、平滑性がない。
[Appearance evaluation]
The obtained foam board was confirmed visually and the external appearance was evaluated according to the following criteria.
○ (Good): No unevenness and smoothness.
X (defect): There is uneven unevenness and there is no smoothness.

[最大点応力、弾性率の測定]
JIS K7171−2008に準拠して、発泡板の最大点応力および弾性率を測定した。
具体的には、テンシロン万能試験機(エー・アンド・デイ社製、商品名「RTG−1310」)を用いて3点押し曲げ試験を行った。測定条件を以下に示す。
試験片サイズ:50mm×150mm。
治具間距離:100mm。
圧縮治具:先端寸法(R)が5mmである圧子と、試験片と接する部分を起点に5°の
傾斜を有する幅100mmの支持台。
圧縮速度:50mm/分。
押し曲げ距離:30mm。
エー・アンド・デイ社製の汎用試験器用データ処理システム MSAT0002RTF/RTGのプログラム中に試験片の厚み、幅、長さを入力した状態で前記3点押し曲げ試験を行い、自動的に算出されるデータとして最大点応力(kPa)、弾性率(MPa)を求めた。
[Measurement of maximum point stress and elastic modulus]
In accordance with JIS K7171-2008, the maximum point stress and elastic modulus of the foamed plate were measured.
Specifically, a three-point press bending test was performed using a Tensilon universal testing machine (trade name “RTG-1310” manufactured by A & D Co., Ltd.). The measurement conditions are shown below.
Test piece size: 50 mm × 150 mm.
Distance between jigs: 100 mm.
Compression jig: an indenter having a tip dimension (R) of 5 mm, and a support base having a width of 100 mm having a 5 ° inclination starting from a portion in contact with the test piece.
Compression speed: 50 mm / min.
Push bending distance: 30 mm.
Data processing system for general-purpose tester manufactured by A & D, Inc. The three-point push bending test is performed with the thickness, width, and length of the test piece entered in the MSAT0002RTF / RTG program, and is automatically calculated. The maximum point stress (kPa) and elastic modulus (MPa) were obtained as data.

[寸法変化の評価]
蒸気発泡(二次発泡)直後の発泡板の表面に、長さ100mmの二本の直線を互いに直交した状態となるように描いた。なお、何れか一本の直線は押出方向に平行となるようにした。次に、発泡板を23℃±3℃、湿度60%±5%の雰囲気下にて1週間に亘って放置した後、二本の直線の長さLをそれぞれ測定し、各直線について下記式に基づいて寸法変化率(%)を算出し、二本の寸法変化率の相加平均値を寸法変化率とした。
寸法変化率(%)=100×(L−100)/100
寸法変化の評価は、以下の基準で行った。
○(良好):蒸気発泡から1週間後で寸法変化率が1%以下。
×(不良):蒸気発泡から1週間後で寸法変化率が1%を超える。
[Evaluation of dimensional change]
Two straight lines having a length of 100 mm were drawn on the surface of the foamed plate immediately after vapor foaming (secondary foaming) so as to be orthogonal to each other. Any one straight line was made parallel to the extrusion direction. Next, the foamed plate was allowed to stand for 1 week in an atmosphere of 23 ° C. ± 3 ° C. and humidity 60% ± 5%, and then the length L of each of the two straight lines was measured. The dimensional change rate (%) was calculated based on the above, and the arithmetic average value of the two dimensional change rates was taken as the dimensional change rate.
Dimensional change rate (%) = 100 × (L−100) / 100
The dimensional change was evaluated according to the following criteria.
○ (Good): The dimensional change rate is 1% or less after one week from the steam foaming.
X (defect): The dimensional change rate exceeds 1% after one week from the steam foaming.

[総合評価]
総合評価は、以下の基準で行った。
○:全ての項目において良好(○)であった場合、総合評価良好。
×:1つの項目でも不良(×)があった場合、総合評価不良。
[Comprehensive evaluation]
Comprehensive evaluation was performed according to the following criteria.
◯: Overall evaluation is good when all items are good (◯).
×: If there is a defect (×) even in one item, the overall evaluation is poor.

[実施例1]
ポリスチレン系樹脂(東洋スチレン社製、商品名「HRM−26」)97.8質量%と、造核剤としてタルクマスターバッチ(竹原化学社製、商品名「MO−60」、PS/タルク(質量比)=40/60)2.2質量%とをドライブレンドした。得られた混合物を第1および第2の2台の押出機を有するタンデム押出機(口径65mm−90mm)のホッパーに供給し、第1押出機内で溶融、混練しつつ、発泡剤としてブタン(イソブタン/ノルマルブタン(質量比)=30/70)をポリスチレン系樹脂100質量部あたり1.2質量部圧入した。さらに溶融混練した溶融混練物を第1押出機から第2押出機に連続的に供給し、第2押出機内の樹脂温度tを発泡に適する166℃まで冷却し、第2押出機先端に接続された口径φ124mmの環状金型から押出した。金型先端温度tは120℃であった。押出された円筒状発泡体をプラグ径403mm、長さ500mmの冷却マンドレルの外周面に沿わせ、冷却マンドレルの左右に設けたカッターで該円筒状発泡体を切開して2枚の発泡シート(一次シート)とした。得られた発泡シート(一次シート)は、厚みが1.2mm、全体密度d3が0.112g/cm、表層密度d4が0.115g/cm、比(d4/d3)が1.03、連続気泡率が5.0体積%であった。
図1に例示した、全長11m、内部温度113℃、蒸気圧0.016MPaのトンネル型蒸気発泡槽内を連続的に通過するように、引取速度13.5m/分の条件で発泡シート(一次シート)を搬送した。該蒸気発泡槽内では、該発泡シートを100℃の水蒸気で加熱して発泡(二次発泡)させた。その後、直径300mm、表面温度35℃の冷却ロールの間を通過させて冷却し、幅620mm、長さ1000mmに裁断して厚み1.85mmのフラットな発泡板を得た。
[Example 1]
97.8% by mass of polystyrene resin (trade name “HRM-26” manufactured by Toyo Styrene Co., Ltd.) and talc masterbatch (trade name “MO-60” manufactured by Takehara Chemical Co., Ltd.), PS / talc (mass by mass) Ratio) = 40/60) 2.2% by mass. The obtained mixture was supplied to a hopper of a tandem extruder (caliber 65 mm-90 mm) having first and second two extruders, and melted and kneaded in the first extruder, butane (isobutane) as a blowing agent. / Normal butane (mass ratio) = 30/70) was pressed into 1.2 parts by mass per 100 parts by mass of the polystyrene resin. Further melt-kneaded product was melt-kneaded was continuously fed from the first extruder to the second extruder, a resin temperature t 1 of the second extruder was cooled to 166 ° C. suitable for foaming, connected to the second end of the extruder It was extruded from an annular mold having a diameter of 124 mm. Die tip temperature t 2 was 120 ° C.. The extruded cylindrical foam is placed along the outer peripheral surface of a cooling mandrel having a plug diameter of 403 mm and a length of 500 mm, and the cylindrical foam is cut by a cutter provided on the left and right sides of the cooling mandrel. Sheet). The obtained foamed sheet (primary sheet) has a thickness of 1.2 mm, an overall density d3 of 0.112 g / cm 3 , a surface layer density d4 of 0.115 g / cm 3 , and a ratio (d4 / d3) of 1.03, The open cell rate was 5.0% by volume.
A foamed sheet (primary sheet) under the conditions of a take-up speed of 13.5 m / min so as to continuously pass through a tunnel-type steam foaming tank having an overall length of 11 m, an internal temperature of 113 ° C., and a steam pressure of 0.016 MPa illustrated in FIG. ) Was transported. In the steam foaming tank, the foamed sheet was heated with 100 ° C. steam to be foamed (secondary foaming). Then, it was cooled by passing between cooling rolls having a diameter of 300 mm and a surface temperature of 35 ° C., and cut into a width of 620 mm and a length of 1000 mm to obtain a flat foamed plate having a thickness of 1.85 mm.

[実施例2〜5]
原料配合、樹脂温度t、金型先端温度t、金型口径、および冷却マンドレルのプラグ径を表1に示すとおりに変更し、蒸気発泡工程の条件を表2に示すように変更した以外は、実施例1と同様にして発泡板を得た。
[Examples 2 to 5]
The raw material composition, resin temperature t 1 , die tip temperature t 2 , die diameter, and cooling mandrel plug diameter were changed as shown in Table 1, and the conditions of the steam foaming process were changed as shown in Table 2. Obtained a foamed plate in the same manner as in Example 1.

[実施例6]
以下のように条件を変更した以外は、実施例1と同様にして発泡板を得た。
原料配合、樹脂温度t、金型先端温度t、金型口径、および冷却マンドレルのプラグ径は表1に示すとおりに変更した。蒸気発泡工程の条件は表2に示すように変更した。さらに図2に例示したように、蒸気発泡槽から出た発泡板の両面に、ホットメルト接着剤(商品名「ヒロダイン7558、ヤスハラケミカル社製)を表面にコーティングしたクラフト紙(厚み0.1mm)をホットメルト接着剤層が発泡板側に来るように積層した。接着用熱ロールの温度は100℃とした。
[Example 6]
A foamed plate was obtained in the same manner as in Example 1 except that the conditions were changed as follows.
The raw material composition, resin temperature t 1 , die tip temperature t 2 , die diameter, and cooling mandrel plug diameter were changed as shown in Table 1. The conditions of the steam foaming process were changed as shown in Table 2. Furthermore, as illustrated in FIG. 2, kraft paper (thickness 0.1 mm) coated with a hot melt adhesive (trade name “Hirodyne 7558, manufactured by Yasuhara Chemical Co., Ltd.) on both surfaces of the foamed plate coming out of the steam foaming tank. The hot melt adhesive layer was laminated so as to be on the foam plate side, and the temperature of the bonding hot roll was set to 100 ° C.

[比較例1〜4]
原料配合、樹脂温度t、金型先端温度t、金型口径、および冷却マンドレルのプラグ径を表1に示すとおりに変更し、蒸気発泡工程の条件を表2に示すように変更した以外は、実施例1と同様にして発泡板を得た。
[Comparative Examples 1-4]
The raw material composition, resin temperature t 1 , die tip temperature t 2 , die diameter, and cooling mandrel plug diameter were changed as shown in Table 1, and the conditions of the steam foaming process were changed as shown in Table 2. Obtained a foamed plate in the same manner as in Example 1.

各例における発泡シート(一次シート)の各測定結果を表1、発泡板の各測定結果および評価結果を表2に示す。
なお、表1における発泡剤の配合量は、ポリスチレン系樹脂100質量部あたりの量を示す。
Each measurement result of the foamed sheet (primary sheet) in each example is shown in Table 1, and each measurement result and evaluation result of the foamed plate are shown in Table 2.
In addition, the compounding quantity of the foaming agent in Table 1 shows the quantity per 100 mass parts of polystyrene resins.

Figure 2015189815
Figure 2015189815

Figure 2015189815
Figure 2015189815

表2に示すように、厚み、比(d2/d1)および連続気泡率がいずれも本発明の条件を満たす実施例1〜6の発泡板は、外観が良好で、製造後の寸法変化が抑制され寸法安定性に優れ、また表面硬度も小さく柔軟性があり、緩衝性を有していた。
一方、連続気泡率が30体積%超で比(d2/d1)が0.8未満である比較例1の発泡板は、表面にムラが生じて外観が不良で、また製造後に寸法が変化してしまい寸法安定性が劣っていた。
連続気泡率が30体積%超である比較例2の発泡板も、外観が不良で、また製造後に寸法が変化してしまい寸法安定性が劣っていた。
連続気泡率が9体積%未満で比(d2/d1)が1.8超である比較例3、4の発泡板は、外観が良好で、寸法安定性に優れるものの、表面硬度が高くなりすぎて柔軟性が劣っていた。
As shown in Table 2, the foamed plates of Examples 1 to 6 in which the thickness, the ratio (d2 / d1), and the open cell ratio all satisfy the conditions of the present invention have good appearance and suppress dimensional changes after production. It was excellent in dimensional stability, had a small surface hardness, was flexible, and had buffering properties.
On the other hand, the foamed plate of Comparative Example 1 having an open cell ratio of more than 30% by volume and a ratio (d2 / d1) of less than 0.8 has a non-uniform appearance on the surface and poor appearance, and the dimensions change after production. The dimensional stability was inferior.
The foamed plate of Comparative Example 2 having an open cell ratio of more than 30% by volume also had a poor appearance, and the dimensions changed after production, resulting in poor dimensional stability.
The foamed plates of Comparative Examples 3 and 4 having an open cell ratio of less than 9% by volume and a ratio (d2 / d1) exceeding 1.8 have good appearance and excellent dimensional stability, but have too high surface hardness. And the flexibility was poor.

本発明の発泡板は、緩衝材、模型飛行機等の玩具、POP用ディスプレイ基板等の様々な用途に好適に使用できる。   The foamed plate of the present invention can be suitably used for various applications such as cushioning materials, toys such as model airplanes, POP display substrates, and the like.

1 発泡シート
2 発泡板
3 紙
4 積層体
10 発泡シートロール
12 ガイドロール
14 蒸気発泡槽
16 冷却ロール
18 裁断機
20 紙ロール
22 接着用熱ロール
DESCRIPTION OF SYMBOLS 1 Foam sheet 2 Foam board 3 Paper 4 Laminated body 10 Foam sheet roll 12 Guide roll 14 Steam foaming tank 16 Cooling roll 18 Cutting machine 20 Paper roll 22 Bonding hot roll

Claims (4)

厚みが1.0〜10mmであり、
全体密度d1に対する、表面から深さ0.2mmまでの表層密度d2の比(d2/d1)が0.8〜1.8であり、
連続気泡率が9〜30体積%である、ポリスチレン系樹脂発泡板。
The thickness is 1.0 to 10 mm,
The ratio (d2 / d1) of the surface layer density d2 from the surface to the depth of 0.2 mm with respect to the total density d1 is 0.8 to 1.8,
A polystyrene-based resin foam board having an open cell ratio of 9 to 30% by volume.
JIS K7171−2008に準拠して3点押し曲げ試験を行ったときの弾性率が10〜30MPaである、請求項1に記載のポリスチレン系樹脂発泡板。   The polystyrene-based resin foamed plate according to claim 1, wherein the elastic modulus is 10 to 30 MPa when a three-point press bending test is performed in accordance with JIS K7171-2008. 請求項1または2に記載されたポリスチレン系樹脂発泡板の製造方法であって、
ポリスチレン系樹脂発泡シートを蒸気で加熱して発泡させ、ポリスチレン系樹脂発泡板を得る工程を有し、
前記ポリスチレン系樹脂発泡シートは、厚みが0.5〜5.0mmであり、全体密度d3に対する、表面から深さ0.2mmまでの表層密度d4の比(d4/d3)が1.0〜1.8であり、連続気泡率が5〜26体積%である、ポリスチレン系樹脂発泡板の製造方法。
A method for producing a polystyrene-based resin foam board according to claim 1 or 2,
Having a step of heating and foaming a polystyrene resin foam sheet with steam to obtain a polystyrene resin foam plate,
The polystyrene-based resin foam sheet has a thickness of 0.5 to 5.0 mm, and a ratio (d4 / d3) of a surface layer density d4 from the surface to a depth of 0.2 mm with respect to the overall density d3 is 1.0 to 1. And a method for producing a polystyrene-based resin foamed plate having an open cell ratio of 5 to 26% by volume.
前記蒸気が水蒸気である、請求項3に記載のポリスチレン系樹脂発泡板の製造方法。   The manufacturing method of the polystyrene-type resin foam board of Claim 3 whose said vapor | steam is water vapor | steam.
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JP7428540B2 (en) 2019-08-06 2024-02-06 株式会社ジェイエスピー Polystyrene resin foam sheet and polystyrene resin laminated foam sheet

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JP2011202007A (en) * 2010-03-25 2011-10-13 Sekisui Plastics Co Ltd Foamed sheet of polystyrene-based resin and method for producing the same
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JPS63122515A (en) * 1986-11-11 1988-05-26 Sekisui Plastics Co Ltd Manufacture of styrene resin foamed sheet
JP2007125830A (en) * 2005-11-05 2007-05-24 Kaneka Corp Laminated expanded sheet of polystyrene-based resin with excellent deep draw forming properties
JP2007217711A (en) * 2007-05-21 2007-08-30 Jsp Corp Polystyrene resin foamed sheet for thermoforming, and polystyrene resin foamed sheet roll for thermoforming
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7428540B2 (en) 2019-08-06 2024-02-06 株式会社ジェイエスピー Polystyrene resin foam sheet and polystyrene resin laminated foam sheet

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