JPS58187436A - Expanded sheet of styrenic resin, having low polymerization degree, and containing rubberlike material - Google Patents

Expanded sheet of styrenic resin, having low polymerization degree, and containing rubberlike material

Info

Publication number
JPS58187436A
JPS58187436A JP7010082A JP7010082A JPS58187436A JP S58187436 A JPS58187436 A JP S58187436A JP 7010082 A JP7010082 A JP 7010082A JP 7010082 A JP7010082 A JP 7010082A JP S58187436 A JPS58187436 A JP S58187436A
Authority
JP
Japan
Prior art keywords
resin
polymerization degree
low polymerization
low
polystyrene resin
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.)
Pending
Application number
JP7010082A
Other languages
Japanese (ja)
Inventor
Masao Nishimura
西村 誠夫
Naohiko Shiozumi
塩住 直彦
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP7010082A priority Critical patent/JPS58187436A/en
Publication of JPS58187436A publication Critical patent/JPS58187436A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:The titled expanded sheet, prepared by incorporating a polystyrenic resin having a low polymerization degree with a rubberlike material, and having a specific expansion ratio, and improved impact resistance and low raw material cost. CONSTITUTION:An expanded sheet obtained by incorporating 100pts.wt. polystyrenic resin having a low polymerization degree, preferably having 0.6<specific viscosity (etasp)<1.1, <=30X10<4> molecular weight and <=10X10<4> polymerization degree, with 0.5-25pts.wt. rubberlike material, e.g. polystyrenic resin prepared by the copolymerization with styrene or graft polymerization with styrene, hot melting the resultant mixture in an extruder, and extruding the melt through an annular slit at the tip thereof into a cylindrical material. The expansion ratio is 3-20.

Description

【発明の詳細な説明】 本発明は新規組成の低重合度ポリスチレン糸樹脂発泡シ
ートに関するものであり、更に詳しくは原料コストが安
価で、耐衝撃性が優れたポリスチレン糸樹脂発泡シート
を提供するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a polystyrene thread resin foam sheet with a new composition, and more specifically, to provide a polystyrene thread resin foam sheet with low raw material cost and excellent impact resistance. It is.

従来より発泡倍率(原料樹脂密度/発泡シート密度)が
3〜20倍のポリスチレン樹脂シートが汎用されている
が、これらポリスチレン樹脂発泡シートはポリスチレン
樹脂がガラス状高分子であるがために機械特性、特に耐
衝撃性に乏しく、例えば他のポリオレフィン系樹脂発泡
体に比べ著しく耐衝撃性が劣り、脆く割れ易いとされて
いる。
Conventionally, polystyrene resin sheets with a foaming ratio (raw resin density/foamed sheet density) of 3 to 20 times have been widely used, but these polystyrene resin foam sheets have poor mechanical properties because the polystyrene resin is a glassy polymer. In particular, it has poor impact resistance, and is said to be significantly inferior to, for example, other polyolefin resin foams, and is brittle and easily cracked.

なかでも低重合度ポリスチレン樹脂については、高重合
度ポリスチレン樹脂よりも比較的製造コストが安価であ
るという長所はあるものの、重合度が低いがゆえに耐衝
撃性もさらに低下し該樹脂による発泡シートは著しく割
れ易く、発泡シートとしての機能を充分に満たすことが
できず、このため該樹脂は使用不可能とされている。
Among these, low-polymerization degree polystyrene resin has the advantage of being relatively cheaper to manufacture than high-polymerization degree polystyrene resin, but because of its low degree of polymerization, its impact resistance further decreases, and foamed sheets made of this resin are The resin is extremely brittle and cannot fully function as a foam sheet, and for this reason, the resin is considered unusable.

これに対する従宋の解決策としては、■高重合度ポリス
チレン樹脂(η、31.として1.3〜1.6程度)を
混合して発泡シートを製造する、(2発泡シートの厚み
を薄くして製造する、■発泡シートの気泡数を増やして
製造する、等が挙げられる。
Concerning Song Dynasty's solutions to this problem were: (1) manufacturing a foam sheet by mixing high polymerization degree polystyrene resin (η, 31. is about 1.3 to 1.6); (2) reducing the thickness of the foam sheet; (2) Producing the foam sheet by increasing the number of cells.

しかしながら、これらの方法では人中な改質効果は望め
ず、さらに■の方法では製造コストが高くなり、■及び
■の方法では発泡シートの成形加工を行なうモルダー(
発泡シートを加熱し軟化させて金型で成形する)のニー
ズに必ずしも合致するとは限らず、例えば成形品の厚み
が薄くなる、発泡シートの熱伝導が低T−’ L加熱効
率が悪化するか、あるいは深−紋り成形が困難になる、
等の大きな欠点があり根本的な解決には今っていない。
However, with these methods, no significant reforming effect can be expected, and method (2) increases the manufacturing cost, and methods (2) and (2) require a molder (which performs the molding process of the foam sheet).
(heating a foam sheet to soften it and molding it with a mold) does not necessarily meet the needs of the molded product, for example, the thickness of the molded product becomes thinner, the thermal conductivity of the foam sheet is low, and the heating efficiency deteriorates. , or it becomes difficult to form deep marks.
There are major drawbacks such as, and no fundamental solution has been found yet.

本発明考らはに記実情に鑑み鋭意研究の結果、低重合度
ポリスチレン樹脂にゴム状物質を含有させることにより
その耐衝撃性が顕著に改質され1゛分実用に1耐え得る
ことを見出し、上記の如きポリスチレン樹脂発泡シート
の欠点を解消したものである。
In view of the current situation, the present invention was conceived and as a result of intensive research, it was discovered that by incorporating a rubber-like substance into a low polymerization degree polystyrene resin, its impact resistance was significantly improved and it could withstand practical use for 1 minute. , which overcomes the drawbacks of polystyrene resin foam sheets as described above.

すなわち、本発明は低重合度ポリスチレン樹脂Vこ」ム
状物質を含有させてなるポリスチレン系樹脂発泡シート
であり、安価なポリスチレン樹脂で製造1■能ゆえ製造
コストが安価で且つ品質的には耐衝撃性の向にしたポリ
スチレン系樹脂発泡シートを提供することを特徴とする
ものである。
That is, the present invention is a polystyrene resin foam sheet containing a low-polymerization degree polystyrene resin V-shaped material, which can be manufactured using inexpensive polystyrene resin, so the manufacturing cost is low and the quality is durable. This invention is characterized by providing a polystyrene resin foam sheet with improved impact resistance.

本発明のポリスチレン系樹脂発泡シートは、通常原料樹
脂と低沸点有機化合物を発泡剤として押出機内で加熱溶
融させ、その先端の環状スリットより筒状体に押出して
製造するものであるが、その発泡剤は押出機に圧入する
方式、或いは予めポリスチレン樹脂に含浸させて発泡性
のポリスチレン樹脂として用いる方式のいずれの場合で
もさしつかえない。
The polystyrene resin foam sheet of the present invention is usually manufactured by heating and melting a raw material resin and a low-boiling organic compound as a foaming agent in an extruder, and extruding it into a cylindrical body through an annular slit at the tip of the extruder. The agent may be press-fitted into an extruder, or it may be impregnated into polystyrene resin in advance and used as a foamable polystyrene resin.

本発明においてゴム状物質が増えると耐衝撃Pigは向
1−二するが、曲げ弾性は低下するという不al(合が
生じる。この場合、[4fi撃性のみ向−Lさせ、曲げ
弾ゼ1−を−・定とすることを期待するには、発泡シー
トの表皮層を押出し直後に空気吹き付は等で冷却するこ
とUこより表皮層をより高密度にすることが必要である
。但し、同時に内層部の密度は低くし、製造した発泡ノ
ート全体としての発泡倍率が面密度層形成のMiJ後で
等しくなるように調整しなければいけない。しかし、一
般的には表皮層をより面密度にすれば成形加1時におい
て成形品が割れる、加熱温度1[1が狭くなる等の弊害
が生じるが、本発明のポリスチレン系樹脂発泡シートに
あってはそれらの点につい一〇も良好な結果を(6)る
ことかできる。
In the present invention, when the rubber-like substance increases, the impact resistance Pig increases in the direction of 1-2, but the bending elasticity decreases. In order to expect - to be constant, it is necessary to make the skin layer of the foam sheet more dense by cooling it with air blowing or the like immediately after extruding it.However, At the same time, the density of the inner layer must be lowered and the foaming ratio of the entire foamed notebook manufactured must be adjusted to be equal after MiJ of areal density layer formation.However, in general, the outer layer should be made with a higher areal density. However, the polystyrene resin foam sheet of the present invention has excellent results in these respects. (6) I can do something.

本発明でいう低重合度ポリスチレン系樹脂とは、比粘度
η、:l爪樹脂1g′トルエン100m/、30 ”C
)が11以i−1分子−t (Mw ) 80 ×l 
O’以1・、重合度い4r、 ) 1’ O’x 10
4以トのものであり、特にη1.l、が0.6より人き
く1.1より小さいものが好ましい1゜ ・!1.発明でいうコ゛ノ、状物質には、1li−1’
;; (合成コム成分かスチレンとグラフト重合してい
るポリスチレン樹脂)、5F31イ、L41..3 H
、ブナゴム、CI(、プチルコ゛ム等の合成ゴムや天然
ゴム、央にはエチレン−酢ビ共重合体等のエラストマー
が包含される。ゴム状物質はスチレンとの共重合もしく
はクラフト状態、またはポリスチレンとのブレンド状態
で存在するが、耐衝撃性の改質効果という点では11J
者の状態が優れている。
In the present invention, the low polymerization degree polystyrene resin refers to a specific viscosity η, :l nail resin 1g'toluene 100m/, 30"C
) is 11 or more i-1 molecule-t (Mw) 80 ×l
O' or more 1., degree of polymerization is 4r, ) 1'O'x 10
4 or more, especially η1. It is preferable that l is smaller than 0.6 and smaller than 1.1. 1. In the invention, the ``cono''-like substance includes 1li-1'
;; (synthetic comb component or polystyrene resin graft-polymerized with styrene), 5F31, L41. .. 3H
Synthetic rubbers and natural rubbers such as , buna rubber, CI (butyl rubber), and elastomers such as ethylene-vinyl acetate copolymer are included. Although it exists in a blended state, it is 11J in terms of impact resistance modification effect.
The condition of the person is excellent.

従って、就中、r(i−、PS 、 S L31イが好
適である。
Therefore, r(i-, PS, S L31i) are particularly suitable.

また、ゴム状物質が25重量部を越えると」−1の曲げ
弾性の低↑゛はさらに著しくなり、寸た原*1のコスト
アップにもなる1、従って、コストメリットかつ耐衝撃
性を同時に満足させるにはゴム状物質の含有率は約0.
5〜約30重駄部が好ましい。
In addition, if the rubber-like substance exceeds 25 parts by weight, the low ↑゛ of the bending elasticity of ``-1'' becomes even more significant, which also increases the cost of the material *1. Therefore, cost benefits and impact resistance can be achieved at the same time. To satisfy the requirements, the content of rubbery substances should be approximately 0.
5 to about 30 double parts are preferred.

以十、実施例により本発明を説明するが、本発明ばこれ
らに限定されず本発明の範囲内で適当に改変することが
できる。
The present invention will be explained below with reference to Examples, but the present invention is not limited to these examples and can be appropriately modified within the scope of the present invention.

実施例1−1 造核剤をブレンドした原料樹脂を発泡剤として用いる低
沸点有機化合物の圧入部を設けてあるl、/l) 二2
5の押出機で圧入した発泡剤とともに220℃で加熱溶
融させ、11.[)= a Oの押出機で150℃に冷
却、その先端の環状スリットより押出し、ポリスチレン
糸樹脂発泡シートを製造した。
Example 1-1 A press-in part for a low-boiling organic compound using a raw material resin blended with a nucleating agent as a blowing agent is provided (l,/l) 22
Heat and melt at 220°C together with the blowing agent press-injected in the extruder in step 5, and 11. [)=a It was cooled to 150° C. using an O extruder and extruded through an annular slit at the tip thereof to produce a polystyrene thread resin foam sheet.

11、i木−1樹脂として、粘材樹脂の低重合度ポリス
チレン樹脂(η:31.’l 019)100市量部、
トI)−1弓樹脂(ゴム成分8型敏%が粘材樹脂である
スチμ/とクラフト重合しているポリスチレン樹脂)5
0市緘部、造核Mlとしてメルク1.3重敏部を均″に
ブレンド〔2、混合物を押出機のポツパーに投入し、押
出機で加熱溶融後、シクロロンフルオ[1メタン10 
!lf量部を圧入し、環状スリットより人気中へ押出し
、直ちに空冷することで発泡シートの表皮層に高密度層
を形成させて厚み2. ]、 ms、シー 1−11’
+ 1−049.、、重紙200 f、ynどのポリス
チレン糸樹脂定泡シートを連続的に製造した。
11, i-Ki-1 resin, 100 parts by weight of low polymerization degree polystyrene resin (η: 31.'l 019) as adhesive resin,
I)-1 Bow resin (polystyrene resin in which the rubber component type 8 is polymerized with styrene, which is a sticky resin) 5
Merck 1.3 heavy duty part was evenly blended as nucleating Ml [2].
! The lf portion is press-fitted, extruded through the annular slit, and immediately cooled in air to form a high-density layer on the skin layer of the foam sheet to a thickness of 2. ], ms, sea 1-11'
+ 1-049. Polystyrene thread resin constant foam sheets such as heavy paper 200 f, yn were manufactured continuously.

′ノご施例1−2 実h1411−1と同一の、原料樹脂を用い、実施例1
−1と同様の操作により発泡シートを製造した。イ11
シ、実施例1−1との差異は表皮層がより高密度である
点で異なる。
Example 1-2 Using the same raw material resin as in Example h1411-1, Example 1
A foamed sheet was manufactured by the same operation as in -1. I11
The difference from Example 1-1 is that the epidermal layer is more dense.

実施例1−3 実施例1−1と同一の低重合度ポリスチレン樹脂及びt
(i、−Pε]樹脂をそれぞれ100及び10屯址部を
原料樹脂として、実施例1−1と同様の操作を行ない発
泡シートを製造した。
Example 1-3 Same low polymerization degree polystyrene resin as Example 1-1 and t
(i, -Pε) Using 100 and 10 tons of the resin as the raw material resin, foamed sheets were produced in the same manner as in Example 1-1.

実施例1−4 実施例1−1と同一の低重合度ポリスチレン樹脂及び1
(ト1″S樹脂をそれぞれ100及び5重111部を原
料樹脂として、実施例1−1と同様の操作を行ない発泡
シートを製造した。
Example 1-4 Low polymerization degree polystyrene resin same as Example 1-1 and 1
(A foamed sheet was manufactured by carrying out the same operation as in Example 1-1 using 100 parts of 1''S resin and 111 parts of 5-weight resin as the raw material resin.

比較例1 実施例1.−1と同=−の低重合度ポリスチレン100
重量部のみを原料樹脂として、実施例1−1と同様の操
作を行ない発泡シートを製造した。
Comparative Example 1 Example 1. Same as -1=-low polymerization degree polystyrene 100
A foamed sheet was manufactured by performing the same operation as in Example 1-1, using only parts by weight as the raw material resin.

比較例2 高重合度ポリスチレン樹脂(ηsp 1.6 ) 10
0屯を迂部のみを11ル料樹脂として実施例1−1と同
様の操作を行ない発泡シートを製造した。
Comparative Example 2 Highly polymerized polystyrene resin (ηsp 1.6) 10
A foamed sheet was produced by carrying out the same operation as in Example 1-1, except that only the round part of the 0 ton was made of 11 resin.

実施例2 造核剤をブレットした原料樹脂をり、、/”D = 3
9の押出機において200 ’Cで加熱溶融させ、その
先端の150 ℃の環状スリットより押出し、ポリスチ
レン糸樹脂発泡シートを製造した。
Example 2 Raw resin pelleted with nucleating agent, /”D = 3
The mixture was melted by heating at 200° C. in an extruder No. 9, and extruded through an annular slit at 150° C. at the tip thereof to produce a polystyrene thread resin foam sheet.

原木」樹脂として、発泡剤の11−ブタ7襠重敏%を含
浸した低重合度ポリスチレン樹脂(ポリスチレン樹脂分
のη、、  −0,9) l O’0重量部1、、p 
一 実施例1−1と同一の1l)−1’s樹脂5o!ti部
、造核剤としてメルク1.8重敏部を均・にブレ。
Low polymerization degree polystyrene resin impregnated with 11-butan 7% foaming agent (polystyrene resin content η, -0,9) l O'0 parts by weight 1, p
1l)-1's resin 5o! same as Example 1-1! Ti part, evenly shake Merck 1.8 heavy duty part as a nucleating agent.

!・し、混合物を押出機のポツパーに投入し、加熱浴融
させ環状スリン1−より人気へ押出し、実施例1−1と
同様の操作を行ない発泡シートを製造した。
! - Then, the mixture was put into the popper of an extruder, melted in a heating bath, extruded through annular Surin 1-1, and the same operation as in Example 1-1 was carried out to produce a foamed sheet.

実施例3 実施例t−tと同一のポリスチレン樹脂lo。Example 3 Polystyrene resin lo same as Example t-t.

市11L部、合成コ゛ム(N 4口() l 9重量部
を原料樹脂として、実施例1−1と同様の操作を行ない
発l包シートを製造した。
An extrusion sheet was produced by carrying out the same operation as in Example 1-1 using 11 liters of plastic and 9 parts by weight of a synthetic comb (4 parts of N) as the raw resin.

実施例4 実施例1−1と同一のポリスチレン樹脂lo。Example 4 Polystyrene resin lo same as Example 1-1.

市鼠部、実施例3と同一の合成ゴム30重量部を原料樹
脂として、実施例1−1と同様の操作を行ない発泡シー
トを製造した。
Using 30 parts by weight of the same synthetic rubber as in Example 3 as a raw material resin, a foamed sheet was produced in the same manner as in Example 1-1.

1−記各実施例及び比較例において得られたポリスチレ
ン糸樹脂発泡シートについて、その品質評価の結果を表
1に示す。
Table 1 shows the results of quality evaluation of the polystyrene thread resin foam sheets obtained in each Example and Comparative Example.

※1)((T)l:安価、○:やや安価、△:やや高価
、×:高価 ※2)数値が大きいほど高密度を形成している。気泡の
形状より判定 ※3)数値が大きいほど#衝撃性あり。落球試験により
判定 ※4)数値が大きいほど曲げ強度が大。一定の歪を生じ
せしめた時の反発力で 判定 ※5)食品包装用のトレイに成形加工 ※6)深絞り成形への適用性、トレイの形状にて判定 ◎:良い、0:やや良い、△:やや 不良、×:不良 表1において、実施例1−1及至1−4.2.3及び4
と比較例1及び2を比較する゛と、ポリスチレン糸樹脂
発泡シートに対するゴム状物質の耐衝撃性の改質効果は
顕著であり、表皮層をより高密度にすることで成形加工
性を低下させることなく、曲げ強度も維持できることが
認められる。また、実施例1−2と実施例2を比較する
ことでその製造方法のいかんにかかわらないことも確認
できる。
*1) ((T)l: Inexpensive, ○: Slightly inexpensive, △: Slightly expensive, ×: Expensive *2) The larger the value, the higher the density. Judging from the shape of the bubbles *3) The higher the number, the more impact resistant it is. Determined by falling ball test *4) The higher the number, the higher the bending strength. Judging by the repulsive force when a certain strain is generated *5) Molding into food packaging trays *6) Applicability to deep drawing molding, judged by the shape of the tray ◎: Good, 0: Fairly good, △: Slightly poor, ×: Poor In Table 1, Examples 1-1 to 1-4.2.3 and 4
Comparing Comparative Examples 1 and 2, it is found that the impact resistance modification effect of the rubber-like substance on the polystyrene thread resin foam sheet is remarkable, and the molding processability is reduced by making the skin layer higher density. It is recognized that the bending strength can also be maintained without any stress. Further, by comparing Examples 1-2 and 2, it can be confirmed that the manufacturing method is not involved.

ゴム状物質の状態については、実施例2と実施例3を比
較することによりポリスチレン樹・脂とブレンドさせる
よりもスナレンと共重合もしくはクラフト重合している
方が好ましいことか理解される。従って、以F二に加え
てコストメリットを考慮すると、1N−1’+;樹脂の
利用が好ましいことが分かる。
Regarding the state of the rubbery substance, by comparing Examples 2 and 3, it can be seen that copolymerization or craft polymerization with sunalene is preferable to blending with polystyrene resin. Therefore, considering the cost merit in addition to F2, it can be seen that it is preferable to use 1N-1'+; resin.

叙」4の如く、本発明は製造コストが安f曲であるのみ
ならず、耐衝撃性に加えて成形性向−にをも顕著に向1
−せしめた新規な低重合度ポリスチレン糸樹脂発泡シー
トを提供するものである。
As shown in Section 4, the present invention not only reduces manufacturing costs but also significantly improves moldability in addition to impact resistance.
- To provide a novel low polymerization degree polystyrene thread resin foam sheet.

Claims (1)

【特許請求の範囲】 1、 低重合度ポリスチレン糸樹脂にゴム状物質を配合
してなり、発泡倍率が8〜20倍である低重合度ポリス
チレン系樹脂シート。 2、 低重合度ポリスチレン系樹脂100重量部に対し
、ゴム状物質0.5〜25重城部を配合してなる特許請
求の範囲第1積重戦の発泡シー ト。 3、低重合度ポリスチレン樹脂成分の比粘度が06〈η
8[、・(1,1である特許請求の範囲第1項又は第2
項記載の発泡シート。 4、 ゴム状物質がスチレンと共重合もしくはクラフト
重合したものである特許請求の範囲第1項又は第2項記
載の発泡シート。
[Scope of Claims] 1. A low polymerization degree polystyrene resin sheet which is made by blending a rubbery substance with a low polymerization degree polystyrene thread resin and has an expansion ratio of 8 to 20 times. 2. A foamed sheet according to claim 1, comprising 0.5 to 25 parts by weight of a rubber-like substance mixed with 100 parts by weight of a low polymerization degree polystyrene resin. 3. The specific viscosity of the low polymerization degree polystyrene resin component is 06〈η
8[,・(1,1) Claim 1 or 2
Foam sheet as described in section. 4. The foamed sheet according to claim 1 or 2, wherein the rubbery substance is copolymerized or kraft polymerized with styrene.
JP7010082A 1982-04-26 1982-04-26 Expanded sheet of styrenic resin, having low polymerization degree, and containing rubberlike material Pending JPS58187436A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7010082A JPS58187436A (en) 1982-04-26 1982-04-26 Expanded sheet of styrenic resin, having low polymerization degree, and containing rubberlike material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7010082A JPS58187436A (en) 1982-04-26 1982-04-26 Expanded sheet of styrenic resin, having low polymerization degree, and containing rubberlike material

Publications (1)

Publication Number Publication Date
JPS58187436A true JPS58187436A (en) 1983-11-01

Family

ID=13421771

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7010082A Pending JPS58187436A (en) 1982-04-26 1982-04-26 Expanded sheet of styrenic resin, having low polymerization degree, and containing rubberlike material

Country Status (1)

Country Link
JP (1) JPS58187436A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53124574A (en) * 1977-04-07 1978-10-31 Japan Styrene Paper Corp Production of foamed polystyrene resin
JPS56109238A (en) * 1980-02-04 1981-08-29 Japan Synthetic Rubber Co Ltd Impact-resistant resin composition

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53124574A (en) * 1977-04-07 1978-10-31 Japan Styrene Paper Corp Production of foamed polystyrene resin
JPS56109238A (en) * 1980-02-04 1981-08-29 Japan Synthetic Rubber Co Ltd Impact-resistant resin composition

Similar Documents

Publication Publication Date Title
US7947754B2 (en) Foam
JP3571352B2 (en) Foamable synthetic resin composition, synthetic resin foam, and method for producing synthetic resin foam
CA2346992C (en) Process for producing extruded polystyrene foam products with co2 containing blowing agents
JP3704034B2 (en) Polypropylene-based resin foam, molded product and method for producing the same
JP2013185074A (en) Polyamide-based resin foamed sheet and method for producing the same
JPS58187436A (en) Expanded sheet of styrenic resin, having low polymerization degree, and containing rubberlike material
JP2001001384A (en) Production of polypropylene resin extruded foamed fine stripe bundle
JP3524006B2 (en) Method for producing polyamide resin foam
JP2008144025A (en) Method for producing styrene-based resin foam sheet
US6809125B1 (en) Foam comprising polyolefin blend and method for producing same
JP2008056863A (en) Polypropylene-based resin foamed sheet and molded article obtained by thermally molding the foamed sheet
JPH1112418A (en) Heat-resistant styrene copolymer composition
JP3812997B2 (en) Extrusion foaming masterbatch, method for producing the same, and method for producing heat-resistant styrene resin foam using the same
JP2004122717A (en) Extruded foam sheet of polypropylene resin, its manufacturing method, and molded product of the same
JP2002037909A (en) Polyester-based resin expanded sheet and method for producing the same
JPH04277508A (en) Rubber-modified styrene resin excellent in strength and transparency
JP2019156880A (en) Heat-resistant styrene-based resin composition, formed product, foam sheet, and food packaging container
JPH01278539A (en) Polypropylene based resin expanded sheet and production thereof
JP2969586B2 (en) Extruded styrene polymer resin foam sheet
JPS6327549A (en) High tenacity highly flexible polymer blend
JP2001055463A (en) Extruded foam sheet of polypropylene-based resin
JPH02184418A (en) Extrusion foaming composition, foaming sheet, manufacture of the same sheet
JP3107569B2 (en) Foamed polyester sheet and method for producing the same
JP3792806B2 (en) Method for producing extruded polycarbonate resin foam
JP3199951B2 (en) Method of adjusting expansion ratio of thermoplastic elastomer foam, method of foaming thermoplastic elastomer, and foam of thermoplastic elastomer