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JPH07106591B2 - Styrene resin foam - Google Patents
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JPH07106591B2 - Styrene resin foam - Google Patents

Styrene resin foam

Info

Publication number
JPH07106591B2
JPH07106591B2 JP2323482A JP32348290A JPH07106591B2 JP H07106591 B2 JPH07106591 B2 JP H07106591B2 JP 2323482 A JP2323482 A JP 2323482A JP 32348290 A JP32348290 A JP 32348290A JP H07106591 B2 JPH07106591 B2 JP H07106591B2
Authority
JP
Japan
Prior art keywords
foam
resin
thickness
thickness direction
extrusion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2323482A
Other languages
Japanese (ja)
Other versions
JPH04189526A (en
Inventor
基滋 林
幹雄 石川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sekisui Kasei Co Ltd
Original Assignee
Sekisui Kasei Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sekisui Kasei Co Ltd filed Critical Sekisui Kasei Co Ltd
Priority to JP2323482A priority Critical patent/JPH07106591B2/en
Publication of JPH04189526A publication Critical patent/JPH04189526A/en
Publication of JPH07106591B2 publication Critical patent/JPH07106591B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/35Component parts; Details or accessories
    • B29C44/352Means for giving the foam different characteristics in different directions

Landscapes

  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は、押し出し発泡によって作られたスチレン系
樹脂発泡体に関するものであり、とくに曲げた状態での
圧縮強度が大きい良質のスチレン系樹脂発泡体に関する
ものである。
Description: TECHNICAL FIELD The present invention relates to a styrene resin foam produced by extrusion foaming, and in particular, a high quality styrene resin foam having a large compressive strength in a bent state. It is about the body.

(従来の技術) スチレン系樹脂発泡体は、色々な分野で使用されてい
る。例えば、薄肉のシートは容器などに加工して使用さ
れ、厚肉の板は畳床、冷凍倉庫の床や壁材などに使用さ
れている。
(Prior Art) Styrenic resin foams are used in various fields. For example, thin sheets are used after being processed into containers and the like, and thick plates are used as tatami floors, floors and wall materials for frozen warehouses, and the like.

スチレン系樹脂発泡体を作るには、押出発泡法が好適で
あることが知られている。押出発泡法とは、押出機を使
用し、押出機内で樹脂を溶融してこれに発泡剤を圧入
し、押出機から押し出すと同時に樹脂を発泡させて、断
面が一様な発泡体を得る方法である。
It is known that an extrusion foaming method is suitable for producing a styrene resin foam. The extrusion foaming method is a method in which a resin is melted in an extruder, a foaming agent is pressed into the extruder, and the resin is foamed at the same time as the resin is extruded from the extruder to obtain a foamed body having a uniform cross section. Is.

発泡剤としては、色々なものが用いられた。その発泡剤
は、次の3種のものに大別された。第1は、樹脂の軟化
点以上の温度で分解して気体を発生する固体化合物であ
る。第2は、樹脂に親和力をもって溶解し、加熱すると
樹脂中で気化する液体又は気体化合物である。第3は、
加圧下に樹脂に溶解することのできる不活性な気体であ
る。このうち、押出発泡法では、第2の樹脂中で気化す
る液体又は気体化合物が最も好んで用いられ、補助的に
第3の不活性な気体が用いられた。
Various foaming agents were used. The foaming agents are roughly classified into the following three types. The first is a solid compound that decomposes at a temperature above the softening point of the resin to generate gas. The second is a liquid or gaseous compound that dissolves in the resin with an affinity and vaporizes in the resin when heated. Third,
It is an inert gas that can dissolve in a resin under pressure. Of these, in the extrusion foaming method, the liquid or gas compound that vaporizes in the second resin was most preferably used, and the third inert gas was used supplementarily.

樹脂中で気化する液体又は気体化合物は、易揮発性液体
とも云われた。易揮発性液体は、これを分けると、ヘキ
サン、ペンタン、ブタンのような脂肪族炭化水素類と、
塩化メチル、ジクロロジフロロメタンのようなハロゲン
化脂肪族炭化水素類との、2種類のものを含んでいた。
不活性な気体は、単に気体とも呼ばれ、二酸化炭素、窒
素などを含んでいた。これらの発泡体は、これを混合し
て用いることとされた。
Liquids or gaseous compounds that vaporize in the resin were also referred to as readily volatile liquids. Easily volatile liquids are divided into aliphatic hydrocarbons such as hexane, pentane and butane,
It contained two types of compounds, halogenated aliphatic hydrocarbons such as methyl chloride and dichlorodifluoromethane.
The inert gas was also simply called a gas and contained carbon dioxide, nitrogen and the like. These foams were to be used as a mixture.

スチレン系樹脂に上述のような発泡剤を加えて押出発泡
を行うと、ここに押出発泡体が得られた。しかし、こう
して得られたスチレン系樹脂発泡体は、曲げ強度と圧縮
強度とが互いに背反する関係を持っていた。すなわち、
圧縮強度の強いものは曲げ強度が弱く、従って僅かに曲
げただけで座屈するようなものとなり、逆に曲げ強度が
強いと、圧縮強度が弱くなる、という関係にあった。ま
た、気泡径を小さくすれば曲げても破断しにくくなる
が、圧縮強度が弱くなった。従って、気泡が小さくて10
%の歪みを加えた条件下で、圧縮強度が2kg/cm2以上と
なるような密度25〜35kg/m3の発泡体は簡単に得られな
かった。
When extrusion foaming was performed by adding the above-mentioned foaming agent to the styrene resin, an extruded foam was obtained. However, in the styrene resin foam thus obtained, the flexural strength and the compressive strength have a contradictory relationship. That is,
There is a relationship that a material having a high compressive strength has a weak bending strength, and therefore becomes buckled even if it is slightly bent, and conversely, if the bending strength is strong, the compressive strength becomes weak. Further, if the bubble diameter was made smaller, it would be less likely to break even when bent, but the compressive strength was weakened. Therefore, the bubbles are small
A foam having a density of 25 to 35 kg / m 3 and having a compressive strength of 2 kg / cm 2 or more could not be easily obtained under the condition that the strain of 100% was added.

ところが、スチレン系樹脂発泡体を使用するがわでは、
当然ながら圧縮強度と曲げ強度とが均衡を保って共にす
ぐれているものを要求していた。例えば、厚肉のスチレ
ン系樹脂発泡板は、畳床の芯材として大量に使用され
た。畳床を製造する際には、厚さ20−25mmの板状の発泡
体を厚さ約300mmに重ねたワラの間に挟み、約50mmの厚
さにロールで圧縮して縫製された。こうしてロールで圧
縮するとき、発泡板の曲げ強度が弱いと破断し、また圧
縮強度が弱いと、所望の厚さの床が得られないこととな
った。従って、或る程度曲げてもその曲げに耐え、曲げ
ても座屈や破断しないで容易に元の状態に戻ることがで
き、しかも曲げた状態でも一応充分な圧縮強度を持って
いるような、スチレン系樹脂発泡体が要求されたが、こ
の要求を満たすような発泡体を確実に得ることはできな
かった。
However, in the case of using styrene resin foam,
As a matter of course, the compressive strength and the bending strength were required to be balanced and excellent. For example, thick styrene resin foam boards have been used in large quantities as core materials for tatami floors. When producing a tatami floor, a plate-like foam having a thickness of 20 to 25 mm was sandwiched between straws having a thickness of about 300 mm and compressed by a roll to a thickness of about 50 mm for sewing. Thus, when compressed by a roll, the foamed plate was broken if the bending strength was weak, and if the compression strength was weak, a floor having a desired thickness could not be obtained. Therefore, even if it is bent to some extent, it can withstand the bending, can easily return to its original state without buckling or breaking even if it is bent, and even if it has a sufficient compression strength even in the bent state, Although a styrene resin foam was required, it was not possible to reliably obtain a foam satisfying this requirement.

スチレン系樹脂を押出発泡させて得られた発泡体は、そ
の表面に必ず非発泡又は低発泡の薄皮を持っていた。従
って、押出発泡体の発泡状態を観察するには、非発泡の
薄皮を剥がして、内部の発泡状態を観察する必要があっ
た。こうして従来の押出発泡体を観察すると、その発泡
状態は区区であった。すなわち、押出発泡の際に採用さ
れる成形条件次第で、色々な気泡状態を現出していた。
例えば、押出発泡の際に押出方向に強く引っ張ると、気
泡はすべて押出方向に引き延ばされたものとなった。ま
た、押出方向の引っ張りを小さくし、厚み方向になるべ
く膨張させるようにすると、気泡は厚み方向に引き延ば
されたものとなった。市場には、このような様々な気泡
状態のものが、入り交じって提供されていた。
The foam obtained by extrusion-foaming a styrene-based resin always had a non-foamed or low-foamed skin on its surface. Therefore, in order to observe the foamed state of the extruded foam, it was necessary to peel off the non-foamed thin skin and observe the foamed state inside. When the conventional extruded foam was observed in this manner, the foamed state was distinct. That is, various bubble states were revealed depending on the molding conditions adopted at the time of extrusion foaming.
For example, when it was strongly stretched in the extrusion direction during extrusion foaming, all the cells were expanded in the extrusion direction. Further, when the tensile force in the extrusion direction was reduced and expanded in the thickness direction as much as possible, the bubbles became elongated in the thickness direction. In the market, various kinds of bubbles are mixedly provided.

(発明が解決しようとする課題) この発明は、密度が25〜35kg/m2のスチレン系樹脂押出
発泡体であって、曲げ強度が強くて、曲げても座屈や破
断を起こさないで容易に元の状態に戻ることができ、し
かも曲げた状態での圧縮強度が大きくて、10%の歪みを
与えた状態での圧縮強度が2kg/cm2以上であるような発
泡体を提供しようとするものである。
(0006) The present invention has a density of a styrene resin extruded foam 25~35kg / m 2, the bending strength is strong, easily without causing buckling or breakage even when bent In order to provide a foam that can return to its original state, has a large compressive strength in a bent state, and a compressive strength of 2 kg / cm 2 or more in a 10% strained state. To do.

(課題解決のための手段) この発明者は、スチレン系樹脂の押出発泡体における圧
縮強度と曲げ強度と関係を検討した。その結果、圧縮強
度と曲げ強度との折衷には、発泡体における気泡状態が
密接に関係していることを突き止めた。
(Means for Solving the Problem) The present inventor examined the relationship between the compressive strength and the bending strength in an extruded foam of a styrene resin. As a result, they found that the compromise between compression strength and bending strength was closely related to the state of bubbles in the foam.

このスチレン系樹脂発泡体は、表面に発泡していない薄
皮を持っているので、気泡状態を観察するには、薄皮を
削り取ってその内部を観察しなければならない。この発
明者は、このようにして発泡体の内部における気泡の状
態と強度との関係を検討した結果、気泡の形状が特別な
状態にあるとき、発泡体は、圧縮強度と曲げ強度とが共
に均衡を保った良好なものとなることを見出した。詳述
すれば、例えば厚さが10〜50mmで密度が25〜35kg/m3
スチレン系樹脂押出発泡板にあっては、薄皮部分として
厚さ1mmを取り除いたとき、表面に現れる気泡が押出方
向に大きく引き延ばされた形になっているが、厚み方向
の中心に近づくに従って、次第に気泡が押出方向に引き
延ばされなくなって、押出方向、幅方向及び厚み方向の
気泡径が等しくなる傾向にあるとき、望ましくは平均気
泡径が0.1−0.5mmのとき、その押出発泡体は圧縮強度と
曲げ強度の双方を均衡に保持したものとなることを見出
した。この発明は、このような知見に基づいて完成され
たものである。
Since this styrene resin foam has a thin skin which is not foamed on the surface, the thin skin must be scraped off and the inside thereof must be observed in order to observe the bubble state. As a result of studying the relationship between the state of bubbles inside the foam and the strength in this way, when the shape of the bubbles is in a special state, the foam has both compressive strength and bending strength. It was found that it would be well balanced and good. More specifically, for example, in the case of a styrene resin extruded foam plate having a thickness of 10 to 50 mm and a density of 25 to 35 kg / m 3 , when the thickness of 1 mm is removed as a thin skin portion, bubbles appearing on the surface are extruded. The shape is greatly extended in the direction, but as it approaches the center of the thickness direction, the bubbles gradually become less extended in the extrusion direction, and the bubble diameters in the extrusion direction, the width direction, and the thickness direction become equal. It has been found that, when tending, and preferably with an average cell size of 0.1-0.5 mm, the extruded foam is balanced in both compressive strength and flexural strength. The present invention has been completed based on such knowledge.

(発明要旨) この発明は、押出発泡法によって作られた薄皮付きのス
チレン系樹脂発泡体であって、厚さが10〜50mm、密度が
25〜35kg/m3であり、表皮から厚さ1mmを除いた部分にお
ける押出方向の平均気泡径が、幅方向及び厚さ方向の平
均気泡径よりも大きく、その比が1.2〜2.0の範囲内にあ
って、その比が発泡体の厚さ方向の中心に近づくに従っ
て、次第に1に近づくことを特徴とする、スチレン系樹
脂発泡体を要旨とするものある。
(Summary of the Invention) The present invention is a styrenic resin foam with a thin skin made by an extrusion foaming method, having a thickness of 10 to 50 mm and a density of
25~35kg / m 3 and average cell diameter of the extrusion direction in a portion excluding the thickness of 1mm from the skin is greater than the average cell diameter in the width direction and the thickness direction, the ratio is in the range of 1.2 to 2.0 The styrene resin foam is characterized in that the ratio gradually approaches 1 as the ratio approaches the center of the foam in the thickness direction.

(各要件の説明) この発明では、樹脂としてスチレン系樹脂を用いる。ス
チレン系樹脂とは、スチレンの単独重合体のほか、スチ
レンと他の単量体との共重合体を含んでいる。他の単量
体は、例えば、α−メチルスチレン、メタクリル酸、ア
クリル酸エステル、メタクリル酸エステル、アクリロニ
トリル、ブタジエン、無水マレイン酸などである。これ
らの共重合体は、スチレンを50重量%以上含むものであ
る。
(Explanation of each requirement) In the present invention, a styrene resin is used as the resin. The styrene-based resin includes a homopolymer of styrene and a copolymer of styrene and another monomer. Other monomers are, for example, α-methylstyrene, methacrylic acid, acrylic acid ester, methacrylic acid ester, acrylonitrile, butadiene, maleic anhydride and the like. These copolymers contain 50% by weight or more of styrene.

押出発泡は、これまで行われて来たように行う。すなわ
ち、スチレン系樹脂にタルクのような無機質充填材を加
え、その他安定剤、顔料、難燃化剤を加え、押出機内で
上述のような発泡剤を圧入して発泡体とする。また、押
出機としては従来の押出機をそのまま使用し、口金とし
てはフラットダイを使用し、さらに口金の先には成形具
を付設して実施することができる。
Extrusion foaming is performed as it has been done so far. That is, an inorganic filler such as talc is added to a styrene resin, other stabilizers, pigments, and flame retardants are added, and the above-mentioned foaming agent is pressed into the extruder to form a foam. A conventional extruder can be used as the extruder as it is, a flat die can be used as the die, and a molding tool can be attached to the tip of the die.

この発明は、スチレン系樹脂発泡体のうち、厚さが10〜
50mmで、密度が25〜35kg/m3の発泡体を対象としてい
る。その理由は、厚さが10mm以下の発泡体では、厚み方
向における気泡の差を正確に把握し難いからであり、厚
さが50mm以上となると気泡の調整が困難となるからであ
る。また、密度が25kg/m3以下では発泡体としての価値
がなく、35kg/m3以上では圧縮強度も曲げ強度も何れも
不充分なものとなるからである。
This invention has a thickness of 10 to 10 among styrene resin foams.
It is intended for foams of 50 mm and density of 25-35 kg / m 3 . The reason is that it is difficult to accurately grasp the difference in bubbles in the thickness direction with a foam having a thickness of 10 mm or less, and it becomes difficult to adjust the bubbles when the thickness is 50 mm or more. Further, if the density is 25 kg / m 3 or less, it is not valuable as a foam, and if it is 35 kg / m 3 or more, both the compressive strength and the bending strength are insufficient.

さらに、平均気泡径については、気泡径が大きいほど圧
縮強度は強くなるが、曲げると破断しやすくなり、また
気泡径が小さいほど曲げても破断しにくくなるが、圧縮
強度は弱くなる。このような点を考慮し、この発明では
平均気泡径を0.1−0.5mmのものとする。
Regarding the average cell diameter, the larger the cell diameter, the stronger the compressive strength, but the more easily it breaks when bent, and the smaller the cell diameter, the harder it becomes to break even if it bends, but the lower the compressive strength. In consideration of such a point, in the present invention, the average bubble diameter is 0.1-0.5 mm.

この発明では、気泡の状態を規定するのに、表皮から厚
さ1mmの薄皮を剥いだ部分を基準とする。それは、前述
のように、押出発泡体が表面に非発泡又は低発泡の薄皮
を持っているからである。この薄皮を剥いだとき、表面
に現れる気泡が押出方向にとくに長く引き延ばされたも
のであることを必要としている。
In the present invention, to define the state of bubbles, the portion where a thin skin having a thickness of 1 mm is peeled from the epidermis is used as a reference. This is because the extruded foam has a non-foamed or low-foamed skin on the surface as described above. When the skin is peeled off, the bubbles appearing on the surface need to be stretched particularly long in the extrusion direction.

具体的には、表面に現れる気泡は、次のような関係にあ
ることを必要としている。押出方向をMDとし、幅方向を
TDとし、厚み方向をVDとすると、MDの平均気泡径がTDの
平均気泡径に対し(MD/TD)、1.2〜2.0の範囲内あり、
またMDの平均気泡径がVDの平均気泡径に対し(MD/V
D)、1.2〜2.0の範囲内にあることを必要としている。
Specifically, the bubbles appearing on the surface need to have the following relationship. The extrusion direction is MD and the width direction is
If TD and VD in the thickness direction, the average bubble diameter of MD is within the range of 1.2 to 2.0 with respect to the average bubble diameter of TD (MD / TD),
Also, the average bubble diameter of MD is (MD / V
D), needs to be in the range 1.2-2.0.

さらに、この発明では、上述のMD/TDの比、及びMD/VDの
比が、何れも発泡体の厚み方向の中心に近づくに従っ
て、次第に1に近づくことを必要としている。このこと
は、云いかえると、発泡体の厚み方向の中心では、気泡
が押出方向にとくに大きく引き延ばされたものでなくな
って、MDがTDに近づくとともにVDにも近づくことを意味
している。発泡体内にある気泡は、その形が角張ってい
て球ではないけれども、球に近い形になっていることを
意味している。
Further, in the present invention, both the MD / TD ratio and the MD / VD ratio described above need to gradually approach 1 as they approach the center of the foam in the thickness direction. In other words, at the center of the foam in the thickness direction, it means that the cells are not particularly stretched in the extrusion direction and MD approaches TD and VD. . The bubbles in the foam mean that they are close to a sphere, though they are angular and not spherical.

上述の関係を図面によってさらに具体的に説明すると、
次のとおりである。第1図ないし第4図は、この発明に
係るスチレン形樹脂押出発泡体の断面拡大図である。第
1図は、表皮から1mmの厚さの表皮を剥いで表面を現
し、この表面から厚さ方向の中心に向かって切断したと
きの発泡体の断面拡大図である。第1図の横方向は押出
方向であり、縦方向は厚さ方向である。第1図の気泡は
横方向に引き延ばされているから、押出方向と厚さ方向
との平均気泡径比は、1.5対1と考えられる。第2図
は、同じ表面を幅方向に表皮から中心に向かって切断し
たときの発泡体の断面拡大図である。第2図の横方向は
幅方向であり、縦方向は厚さ方向である。第1図の押出
方向の気泡径は、第2図の幅方向の気泡径より大きく、
その平均気泡径比は1.2対1と考えられる。
The above relationship will be described more specifically with reference to the drawings.
It is as follows. 1 to 4 are enlarged sectional views of a styrene type resin extruded foam according to the present invention. FIG. 1 is an enlarged cross-sectional view of a foam when a surface of 1 mm in thickness is peeled from the surface to reveal the surface and the surface is cut toward the center in the thickness direction. The horizontal direction in FIG. 1 is the extrusion direction, and the vertical direction is the thickness direction. Since the bubbles in FIG. 1 are stretched in the lateral direction, the average bubble diameter ratio in the extrusion direction and the thickness direction is considered to be 1.5: 1. FIG. 2 is an enlarged cross-sectional view of the foam when the same surface is cut in the width direction from the epidermis toward the center. The horizontal direction in FIG. 2 is the width direction, and the vertical direction is the thickness direction. The bubble diameter in the extrusion direction in FIG. 1 is larger than the bubble diameter in the width direction in FIG.
The average bubble diameter ratio is considered to be 1.2: 1.

第3図は、第1図及び第2図と同じ発泡体を厚み方向の
中心部において、厚さ方向に切断したときの断面を、第
1図及び第2図と同じ倍率に拡大して示したものであ
る。第3図の横方向は押出方向であり、縦方向は厚さ方
向である。第3図では気泡の平均径が、押出方向と厚さ
方向とで1.06対1の比となっている。第4図は、同じ発
泡体の厚み方向の中心部において幅方向に切断したとき
の断面拡大図である。第4図の横方向は幅方向であり、
縦方向は厚さ方向である。第3図の押出方向の気泡径は
第4図の幅方向の気泡径より大きく、その平均径が、1.
1対1の比となっている。
FIG. 3 shows a cross-section of the same foam as that shown in FIGS. 1 and 2 when cut in the thickness direction at the central portion in the thickness direction, enlarged to the same magnification as in FIGS. 1 and 2. It is a thing. The horizontal direction in FIG. 3 is the extrusion direction, and the vertical direction is the thickness direction. In FIG. 3, the average diameter of bubbles is 1.06: 1 in the extrusion direction and the thickness direction. FIG. 4 is an enlarged cross-sectional view of the same foam in the widthwise direction at the center in the thickness direction. The horizontal direction in FIG. 4 is the width direction,
The vertical direction is the thickness direction. The bubble diameter in the extrusion direction in Fig. 3 is larger than the bubble diameter in the width direction in Fig. 4, and the average diameter is 1.
The ratio is 1: 1.

第5図ないし第8図は、この発明に係る他のスチレン系
樹脂発泡体の断面拡大図である。第5図及び第6図は、
第1図及び第2図と同様に、表皮を除いたあとの表面部
において、それぞれ厚さ方向及び幅方向に切断したとき
の発泡体断面の拡大図である。第5図の横方向は押出方
向であり、縦方向は厚さ方向である。第5図では、平均
気泡径が押出方向と厚さ方向とで0.33対0.22の比となっ
ている。第6図の横方向は幅方向であり、縦方向は厚さ
方向である。第5図の押出方向の気泡径は第6図の幅方
向の気泡径より大きく、その比は0.33対0.20となってい
る。
5 to 8 are enlarged sectional views of other styrene resin foams according to the present invention. 5 and 6 show
FIG. 3 is an enlarged view of a foam cross section when cut in the thickness direction and the width direction, respectively, in the surface portion after removing the skin, as in FIGS. 1 and 2. The horizontal direction in FIG. 5 is the extrusion direction, and the vertical direction is the thickness direction. In FIG. 5, the average bubble diameter has a ratio of 0.33 to 0.22 in the extrusion direction and the thickness direction. The horizontal direction in FIG. 6 is the width direction, and the vertical direction is the thickness direction. The bubble diameter in the extrusion direction in FIG. 5 is larger than the bubble diameter in the width direction in FIG. 6, and the ratio is 0.33 to 0.20.

第7図及び第8図は、第3図及び第4図と同様に、発泡
体の厚み方向の中心部において、それぞれ厚さ方向及び
幅方向に切断したときの断面を第5図及び第6図と同じ
倍率に拡大した図である。第7図の横方向は押出方向を
示し、縦方向は厚さ方向を示している。第7図では、気
泡径が押出方向と厚さ方向とで0.37対0.35の比となって
いる。第8図の横方向は幅方向を示し、縦方向は厚さ方
向を示している。第7図の押出方向の気泡径は第8図の
幅方向の気泡径より大きく、その比は0.37対0.35の比と
なっている。
Similar to FIGS. 3 and 4, FIGS. 7 and 8 are cross-sectional views taken along the thickness direction and the width direction at the center of the foam in the thickness direction, respectively. It is the figure expanded to the same magnification as the figure. The horizontal direction in FIG. 7 indicates the extrusion direction, and the vertical direction indicates the thickness direction. In FIG. 7, the bubble diameter has a ratio of 0.37 to 0.35 in the extrusion direction and the thickness direction. The horizontal direction in FIG. 8 indicates the width direction, and the vertical direction indicates the thickness direction. The bubble diameter in the extrusion direction in FIG. 7 is larger than the bubble diameter in the width direction in FIG. 8, and the ratio is 0.37 to 0.35.

(発明の効果) 上述のような気泡を持ったスチレン系樹脂の押出発泡体
は、曲げ強度に対し圧縮強度が均衡の取れた充分なもの
となっていることを特徴としている。このことは、上述
の発泡体に10%の歪みを加えたときの圧縮強度を測定す
ると、明らかである。すなわち、これまでのスチレン系
樹脂の押出発泡体は、10%の歪みを加えてその圧縮強度
を測定すると、その圧縮強度は2kg/cm2未満であった
が、この発明に係る押出発泡体は2kg/cm2以上の10%歪
み圧縮強度を持っている。従って、この発明に係る発泡
体は、曲げ強度と圧縮強度とが共に必要とされる分野、
畳床の芯材、とくにワラと複合して使用する分野におい
て有用な材料となり、各方面の用途が期待される。
(Effects of the Invention) The styrene resin extruded foam having bubbles as described above is characterized in that the compression strength is well balanced with the bending strength. This is clear when measuring the compressive strength of the above foam when a strain of 10% is applied. That is, the extruded foam of styrene resin until now, when the compressive strength was measured by applying a strain of 10%, the compressive strength was less than 2 kg / cm 2 , but the extruded foam according to the present invention is It has a 10% strain compression strength of 2 kg / cm 2 or more. Therefore, the foam according to the present invention is a field in which both bending strength and compressive strength are required,
It is a useful material in the field where it is used in combination with the core material of tatami floors, especially straw, and is expected to be used in various fields.

以下に実施例を挙げて、この発明に係る発泡体のすぐれ
ている所以を具体的に明らかにする。以下の実施例にお
いて、単に部又は%というのは、重量部又は重量%の意
味である。また、平均気泡系の測定は、ASTM−D2842−6
9によって測定した。
Hereinafter, the reason why the foam according to the present invention is excellent will be specifically described with reference to examples. In the examples below, simply parts or% means parts by weight or% by weight. In addition, the average bubble system is measured by ASTM-D2842-6
Measured by 9.

実施例1 樹脂としてポリスチレン(ビカット軟化点103℃、メル
トインデックス4.5)を用い、この樹脂100部に対して、
粒径1〜4ミクロンの微粉末タルク5.0部と、臭素系の
難燃化剤としてヘキサブロモシクロドデカン2部と、ト
リスノニルフェニルフォスファイト0.05部とを加え、こ
の混合物を押出機に供給した。
Example 1 Polystyrene (Vicat softening point 103 ° C., melt index 4.5) was used as a resin, and with respect to 100 parts of this resin,
5.0 parts of fine powder talc having a particle size of 1 to 4 microns, 2 parts of hexabromocyclododecane as a brominated flame retardant, and 0.05 parts of trisnonylphenyl phosphite were added, and this mixture was fed to the extruder.

押出機内で上記混合物を加熱溶融して混合するととも
に、溶融樹脂に発泡剤を圧入した。発泡剤としてはメチ
ルクロライドだけを用い、樹脂1Kgに対してメチルクロ
ライドを2.4モル圧入した。
The above mixture was heated and melted in an extruder to be mixed, and a foaming agent was pressed into the molten resin. Only methyl chloride was used as the foaming agent, and 2.4 mol of methyl chloride was injected under pressure to 1 kg of the resin.

押出機の出口で樹脂の温度を125℃に調整し、口金から
押し出した。口金としては、先端に厚さ0.5mm、幅100mm
の細隙を穿設し、ここから樹脂を押し出すものを用い
た。口金の先端には成形具を密接して取付けた。成形具
としては、入口寸法が口金の上記細隙に実質的に等し
く、出口寸法が厚さ22mm、幅200mmで全長が50mmであ
り、入口から出口に向かつてゆるやかに拡大された樹脂
通路を備えたものを用いた。この樹脂通路には内面に弗
素樹脂が被覆されていた。成形具には90℃の油を循環さ
せて冷却した。このようにして口金から出た樹脂を成形
具へ導き、これをロールで押圧しながら引取り、厚さ25
mm、幅約250mmの押出発泡板を得た。
The temperature of the resin was adjusted to 125 ° C. at the outlet of the extruder and extruded from the die. As a base, the tip is 0.5 mm thick and 100 mm wide
Was used, and the resin was extruded from there. A molding tool was closely attached to the tip of the die. The molding tool has an inlet dimension substantially equal to the above-mentioned slit of the die, an outlet dimension of 22 mm in thickness, a width of 200 mm and a total length of 50 mm, and is provided with a resin passage that is gradually expanded from the inlet to the outlet. I used the one. The inside of this resin passage was coated with a fluororesin. Oil at 90 ° C was circulated in the molding tool to cool it. In this way, the resin that came out of the die is guided to the molding tool, and it is taken up while pressing it with a roll to a thickness of 25
An extruded foam plate having a width of 250 mm and a width of about 250 mm was obtained.

得られた発泡板は、密度が32Kg/m3で、薄皮1mmを除いた
部分の平均気泡径が0.3mmで、薄皮1mm直下の気泡は長手
方向(MD)が0.29mm、幅方向(TD)が0.24mm、厚さ方向
(VD)が0.19mmであつた。従つてMD/TD=1.2、MD/VD=
1.5で厚さ方向中心の気泡はMDが0.37mm、TDが0.32mm、V
Dが0.35mmであり、MD/TD=1.1、MD/VD=1.06で、常温で
2週間放置後に厚さ方向に10%歪を加えたときの圧縮強
度は2.5Kg/cm2であつた。また、20℃における熱伝導率
は0.029Kcal/m・hr・℃であつて、ワラと複合して破
断、座屈することなく、良好な畳床に加工することがで
き、また断熱材としても良好なものであつた。
The resulting foam plate had a density of 32 kg / m 3 , an average cell diameter of 0.3 mm excluding the skin 1 mm, and the cells immediately below the skin 1 mm had a longitudinal direction (MD) of 0.29 mm and a width direction (TD). Was 0.24 mm and the thickness direction (VD) was 0.19 mm. Therefore, MD / TD = 1.2, MD / VD =
At 1.5, the bubble in the thickness direction center is MD 0.37mm, TD 0.32mm, V
D was 0.35 mm, MD / TD = 1.1, MD / VD = 1.06, and the compressive strength was 2.5 kg / cm 2 when 10% strain was applied in the thickness direction after standing for 2 weeks at room temperature. In addition, the thermal conductivity at 20 ℃ is 0.029Kcal / m ・ hr ・ ℃, and it can be processed into a good tatami floor without breaking and buckling in combination with straws, and also as a heat insulating material. It was natural.

実施例2 実施例1において、樹脂100部に対し平均粒径1.5〜1.8
ミクロンの微粉末タルクを4.0部用い、メチルクロライ
ドを樹脂1Kgに対して3モルに用いることとした以外
は、実施例1と全く同様にして発泡板を得た。
Example 2 In Example 1, the average particle size is 1.5 to 1.8 with respect to 100 parts of the resin.
A foam plate was obtained in exactly the same manner as in Example 1 except that 4.0 parts of micronized talc powder was used and methyl chloride was used in an amount of 3 mol per 1 kg of the resin.

得られた発泡板は、密度が30Kg/m3で、薄皮1mmを除いた
部分の平均気泡径が0.35mm、薄皮1mm直下の気泡はMD/TD
/VDの比が0.33/0.25/0.20であり、厚さ方向の中心にお
いてMD/TD/VDの比が0.37/0.35/0.35であり、常温で2週
間放置後に、厚さ方向に10%の歪を加えたときの圧縮強
度が2.4Kg/m2であつた。従つて、実施例1と同様に、畳
床芯材、断熱材として良好な発泡体と認められた。
The resulting foam plate had a density of 30 kg / m 3 , an average cell diameter of 0.35 mm excluding the skin 1 mm, and the cells immediately below the skin 1 mm were MD / TD.
The ratio of / VD is 0.33 / 0.25 / 0.20, the ratio of MD / TD / VD is 0.37 / 0.35 / 0.35 at the center of the thickness direction, and the strain of 10% in the thickness direction after leaving for 2 weeks at room temperature. The compressive strength when added was 2.4 Kg / m 2 . Therefore, as in Example 1, it was recognized that the foam was good as a tatami-bed core material and a heat insulating material.

実施例3 実施例1において、樹脂100部に対し微粉末タルクを3.5
部用い、発泡剤として樹脂1Kgに対しメチルクロライド
2モルと窒素ガス0.1モルとの混合物を用いることとし
た以外は、実施例1と全く同様にして発泡板を得た。
Example 3 In Example 1, 3.5 parts of fine powder talc was added to 100 parts of the resin.
A foam plate was obtained in exactly the same manner as in Example 1 except that a mixture of 2 mol of methyl chloride and 0.1 mol of nitrogen gas was used as a foaming agent per 1 kg of the resin.

得られた発泡板は、密度が32Kg/m3で、薄皮1mmを除いた
部分の平均気泡径が0.28mm、薄皮1mm直下の気泡はMD/TD
/VDの比が0.33/0.28/0.21であり、厚さ方向の中心にお
いてMD/TD/VDの比が0.31/0.26/0.31であり、常温で2週
間放置後に、厚さ方向に10%の歪を加えたときの圧縮強
度が2.5Kg/m2であつた。従つて、実施例1と同様に、畳
床芯材、断熱材として良好な発泡体と認められた。
The resulting foam plate had a density of 32 kg / m 3 , an average cell diameter of 0.28 mm excluding the skin 1 mm, and the cells immediately below the skin 1 mm were MD / TD.
The ratio of / VD is 0.33 / 0.28 / 0.21, the ratio of MD / TD / VD is 0.31 / 0.26 / 0.31 at the center of the thickness direction, and the strain of 10% in the thickness direction after leaving for 2 weeks at room temperature. The compressive strength when added was 2.5 Kg / m 2 . Therefore, as in Example 1, it was recognized that the foam was good as a tatami-bed core material and a heat insulating material.

実施例4 実施例1において、樹脂1Kgに対しメチルクロライド2
モルと、モノクロロジフロロメタン0.2モルとを用いる
こととした以外は、実施例1と全く同様にして発泡板を
得た。
Example 4 In Example 1, 2 kg of methyl chloride was added to 1 kg of the resin.
A foam plate was obtained in exactly the same manner as in Example 1 except that 1 mol and 0.2 mol of monochlorodifluoromethane were used.

得られた発泡板は、密度が29Kg/m3で、薄皮1mmを除いた
部分の平均気泡径が0.31mm、薄皮1mm直下の気泡はMD/TD
/VDの比が0.42/0.36/0.23であり、厚さ方向の中心にお
いてMD/TD/VDの比が0.47/0.34/0.38であり、常温で2週
間放置後に厚さ方向に10%の歪を加えたときの圧縮強度
が2.0Kg/cm2であつて、実施例1と同様に、畳床芯材、
断熱材として良好と認められた。
The foam plate obtained had a density of 29 kg / m 3 , an average cell diameter of 0.31 mm excluding the skin 1 mm, and the cells immediately below the skin 1 mm were MD / TD.
The ratio of / VD is 0.42 / 0.36 / 0.23, the ratio of MD / TD / VD is 0.47 / 0.34 / 0.38 at the center of the thickness direction, and the strain of 10% is applied in the thickness direction after left at room temperature for 2 weeks. The compressive strength when added was 2.0 kg / cm 2 , and as in Example 1, the tatami mat core material,
It was recognized as good as a heat insulating material.

比較例1 実施例1において、樹脂100部に対し微粉末タルクを1.0
部用い、発泡剤として樹脂1Kgに対しメチルクロライド
を2モル用いることとした以外は、実施例1と全く同様
にして発泡板を得た。
Comparative Example 1 In Example 1, 1.0 part of fine powder talc was added to 100 parts of the resin.
A foam board was obtained in exactly the same manner as in Example 1, except that 2 mol of methyl chloride was used per 1 kg of resin as the foaming agent.

得られた発泡板は、密度が36Kg/m3で、薄皮1mmを剥いだ
部分の平均気泡径が0.9mmで薄皮1mm直下の気泡は、MD/T
D/VDの比が1.0/0.9/0.6であり、厚さ方向の中心におけ
るMD/TD/VDの比が1.2/1.0/0.7であり、常温で2週間放
置後に、厚さ方向に10%の歪を加えたときの圧縮強度が
1.6Kg/cm2であつた。従つて、この発泡体は実施例1〜
3のものに比べて劣るものであつた。
The resulting foam plate has a density of 36 kg / m 3 , an average bubble diameter of 0.9 mm in the part where the thin skin 1 mm was peeled off, and the bubbles immediately below the thin skin 1 mm were MD / T.
The ratio of D / VD is 1.0 / 0.9 / 0.6, the ratio of MD / TD / VD in the center of the thickness direction is 1.2 / 1.0 / 0.7, and it is 10% in the thickness direction after left at room temperature for 2 weeks. Compressive strength when strain is applied
It was 1.6 Kg / cm 2 . Therefore, this foam has
It was inferior to that of No. 3.

比較例2 実施例1において、樹脂100部に対し平均粒径が15ミク
ロンの微粉末タルクを4.0部用い、発泡剤として樹脂1Kg
に対しメチルクロライドを2モル用いることとした以外
は、実施例1と全く同様にして発泡板を得た。
Comparative Example 2 In Example 1, 4.0 parts of fine powder talc having an average particle size of 15 microns was used for 100 parts of resin, and 1 kg of resin was used as a foaming agent.
On the other hand, a foam plate was obtained in exactly the same manner as in Example 1 except that 2 mol of methyl chloride was used.

得られた発泡板は、密度が33Kg/m3で、薄皮1mmを剥いだ
部分の平均気泡径が0.42mmで、薄皮1mm直下の気泡はMD/
TD/VDの比が0.4/0.25/0.18であり、厚さ方向の中心にお
けるMD/TD/VDの比が0.61/0.3/0.28であり、常温で2週
間放置後に、厚さ方向に10%の歪を加えたときの圧縮強
度が1.5Kg/cm2であつた。従つて、この発泡体は実施例
1〜3のものに比べて劣るものであつた。
The obtained foam plate has a density of 33 Kg / m 3 , an average cell diameter of 0.42 mm in the part where the thin skin 1 mm is peeled off, and the bubbles directly below the thin skin 1 mm are MD /
The ratio of TD / VD is 0.4 / 0.25 / 0.18, the ratio of MD / TD / VD in the center of the thickness direction is 0.61 / 0.3 / 0.28, and it is 10% in the thickness direction after being left at room temperature for 2 weeks. The compressive strength when strained was 1.5 Kg / cm 2 . Therefore, this foam was inferior to those of Examples 1 to 3.

【図面の簡単な説明】 第1図及び第2図は、この発明に係る発泡体の表皮から
厚さ1mmの部分を剥いで現れた表面部分の発泡体の断面
拡大図である。第3図及び第4図は、同じ発泡体の厚さ
方向の中心部における発泡体断面の拡大図である。第5
図及び第6図は、この発明に係る他の発泡体の表皮から
厚さ1mmの部分を剥いで現れた表面部分の発泡体の断面
拡大図である。第7図及び第8図は、同じ発泡体の厚さ
方向の中心部における発泡体断面の拡大図である。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 and FIG. 2 are enlarged cross-sectional views of the foamed portion of the surface of the foamed body according to the present invention, where a 1 mm-thickness portion is peeled from the skin. FIG. 3 and FIG. 4 are enlarged views of the foam cross section at the central portion in the thickness direction of the same foam. Fifth
FIG. 6 and FIG. 6 are enlarged cross-sectional views of the foamed portion of the surface portion which appears by peeling off a portion having a thickness of 1 mm from the skin of another foamed material according to the present invention. FIG. 7 and FIG. 8 are enlarged views of the foam cross section at the central portion in the thickness direction of the same foam.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】押出発泡法によって作られた薄皮付きのス
チレン系樹脂発泡体であって、厚さが10〜50mm、密度が
25〜35kg/m3であり、表皮から厚さ1mmを除いた部分にお
ける押出方向の平均気泡径が、幅方向及び厚み方向の平
均気泡径よりも大きく、その比が1.2〜2.0の範囲内にあ
って、その比の値が発泡体の厚さ方向の中心に近づくに
従って、次第に1に近づくことを特徴とする、スチレン
系樹脂発泡体。
1. A styrenic resin foam with a thin skin, produced by an extrusion foaming method, having a thickness of 10 to 50 mm and a density of
25 ~ 35 kg / m 3 , the average cell diameter in the extrusion direction in the portion excluding the thickness 1 mm from the skin is larger than the average cell diameter in the width direction and the thickness direction, the ratio is within the range of 1.2 to 2.0. A styrene-based resin foam, wherein the value of the ratio gradually approaches 1 as it approaches the center of the foam in the thickness direction.
JP2323482A 1990-11-26 1990-11-26 Styrene resin foam Expired - Fee Related JPH07106591B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2323482A JPH07106591B2 (en) 1990-11-26 1990-11-26 Styrene resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2323482A JPH07106591B2 (en) 1990-11-26 1990-11-26 Styrene resin foam

Publications (2)

Publication Number Publication Date
JPH04189526A JPH04189526A (en) 1992-07-08
JPH07106591B2 true JPH07106591B2 (en) 1995-11-15

Family

ID=18155183

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2323482A Expired - Fee Related JPH07106591B2 (en) 1990-11-26 1990-11-26 Styrene resin foam

Country Status (1)

Country Link
JP (1) JPH07106591B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09206669A (en) * 1996-01-31 1997-08-12 Sekisui Plastics Co Ltd Polystyrene foam sheet and method for producing the same
AU5900699A (en) 1998-08-28 2000-03-21 Dow Chemical Company, The Fire resistant styrene polymer foams with reduced brominated fire retardant
JP4540027B2 (en) * 2000-02-08 2010-09-08 株式会社ジェイエスピー Open cell foam, vacuum insulation core material and vacuum insulation material
JP5365902B2 (en) * 2008-09-05 2013-12-11 株式会社カネカ Roll receiver made of styrene resin foam plate
JP2010058823A (en) * 2008-09-05 2010-03-18 Kaneka Corp Method for manufacturing roll receiver consisting of styrene resin foam plate
JP2010083485A (en) * 2008-09-08 2010-04-15 Kaneka Corp Method for manufacturing roll receiving tool using cellular orientation styrene resin foaming board
JP2010083484A (en) * 2008-09-08 2010-04-15 Kaneka Corp Roll receiving tool using styrene resin extrusion foaming board
JP5478320B2 (en) * 2010-03-25 2014-04-23 積水化成品工業株式会社 Polystyrene resin foam sheet
BR112017013539A2 (en) * 2014-12-22 2018-03-06 Basf Se anisotropic foam fiber reinforcement
JP6826982B2 (en) * 2014-12-22 2021-02-10 ビーエイエスエフ・ソシエタス・エウロパエアBasf Se Reinforced with fibers of foam manufactured from segments joined together

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JPS5956024U (en) * 1982-10-08 1984-04-12 積水化成品工業株式会社 sheet foam
JPS59152039U (en) * 1983-03-31 1984-10-12 日本スチレンペ−パ−株式会社 Core material for tatami flooring
JPH0661861B2 (en) * 1987-06-29 1994-08-17 積水化成品工業株式会社 Flexible styrenic resin foam board and method for producing the same

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