JP2774814B2 - Method for producing highly elastic thermoplastic resin foam molded article - Google Patents

Method for producing highly elastic thermoplastic resin foam molded article

Info

Publication number
JP2774814B2
JP2774814B2 JP12087589A JP12087589A JP2774814B2 JP 2774814 B2 JP2774814 B2 JP 2774814B2 JP 12087589 A JP12087589 A JP 12087589A JP 12087589 A JP12087589 A JP 12087589A JP 2774814 B2 JP2774814 B2 JP 2774814B2
Authority
JP
Japan
Prior art keywords
molded article
foam molded
compression
foam
thermoplastic 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.)
Expired - Fee Related
Application number
JP12087589A
Other languages
Japanese (ja)
Other versions
JPH02299821A (en
Inventor
一生 浅野
Original Assignee
三菱化学ビーエーエスエフ株式会社
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 三菱化学ビーエーエスエフ株式会社 filed Critical 三菱化学ビーエーエスエフ株式会社
Priority to JP12087589A priority Critical patent/JP2774814B2/en
Publication of JPH02299821A publication Critical patent/JPH02299821A/en
Application granted granted Critical
Publication of JP2774814B2 publication Critical patent/JP2774814B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 (発明の目的) 本発明は、反撥弾性、緩衝性、二次加工性に優れた高
弾性のポリスチレン、ポリエチレン、ポリプロピレン、
ポリアミド等の熱可塑性樹脂発泡成形品の製造方法を提
供するものである。
DETAILED DESCRIPTION OF THE INVENTION (Object of the Invention) The present invention relates to highly elastic polystyrene, polyethylene, polypropylene, and the like having excellent rebound resilience, cushioning properties, and secondary workability.
An object of the present invention is to provide a method for producing a foamed molded article of a thermoplastic resin such as polyamide.

(産業上の利用分野) 本発明の製造方法により得られた高弾性の発泡成形品
は、床下地材、貯蔵タンクの断熱材、建築壁断熱材、バ
ンパー芯材、包装緩衝材として有用である。
(Industrial Application Field) The highly elastic foam molded product obtained by the production method of the present invention is useful as a floor covering material, a heat insulating material for a storage tank, a heat insulating material for a building wall, a bumper core material, and a packaging cushioning material. .

(従来技術) 従来、発泡スチレン系樹脂成形品は軽量性及び断熱性
に優れていることから緩衝包装材、容器等に幅広く使用
されている。しかしながら圧縮歪が大きく、又、反撥弾
性に劣る欠点とともに割れ易く溝切加工、釣り鐘状、円
筒状に打ち抜く加工等のような複雑な機械加工を行うこ
とができない等の欠点があつた。
(Prior art) Conventionally, foamed styrenic resin molded articles have been widely used for cushioning packaging materials, containers and the like because of their excellent lightness and heat insulating properties. However, there are drawbacks such as a large compressive strain, a defect of poor rebound resilience, and a difficulty in performing complicated mechanical processing such as grooving, bell-shaped or cylindrical punching because of easy cracking.

このスチレン系樹脂成形品の弾性に乏しい欠点を改良
する方法として、スチレン系樹脂の予備発泡粒子をモー
ルド内に充填し、前記予備発泡粒子をスチームにより加
熱して膨張させると共に、相互に融着させて発泡スチレ
ン系樹脂成形品となし、該発泡スチレン系樹脂成形品を
モールドより脱型し、熟成させ、次いで該発泡スチレン
系樹脂成形品を型枠内に入れ、プレス機にて圧縮歪が25
〜50%となるように圧縮することを特徴とする高弾性発
泡スチレン系樹脂成形品の製造方法が提案された(特公
昭61−34378号)。
As a method for improving the poor elasticity of the styrene resin molded article, pre-expanded particles of styrene resin are filled in a mold, and the pre-expanded particles are expanded by heating with steam and fused together. To form a foamed styrene-based resin molded product, remove the foamed styrene-based resin molded product from the mold, ripen, and then put the foamed styrene-based resin molded product in a mold frame.
A method for producing a highly elastic foamed styrenic resin molded article characterized by being compressed to 50% or less has been proposed (JP-B-61-34378).

(発明が解決しようとする課題) この方法により得られる成形品は弾性に優れ、圧縮解
放後の戻り寸法にも優れるものであるが、次の欠点があ
る。
(Problems to be Solved by the Invention) The molded article obtained by this method is excellent in elasticity and excellent in return dimensions after compression release, but has the following disadvantages.

(i).型内ビーズ発泡成形品を圧縮し、圧縮を解放
し、再び圧縮をし、再び圧縮を解放するという作業を3
〜6回繰り返さなければ短時間で高弾性の発泡成形品と
することができない。
(I). The work of compressing the bead in-mold foamed product, releasing the compression, compressing again, and releasing the compression again is performed in three steps.
Unless it is repeated up to 6 times, a highly elastic foam molded article cannot be obtained in a short time.

(ii).型内ビーズ発泡成形品の密度が11.6g/や16.8
g/のように発泡倍率が60〜100倍と高発泡のものは、
圧縮時に型内ビーズ発泡成形品の肉厚が80%減じられる
まで圧縮できるが、型内ビーズ発泡成形品の密度が30〜
100g/と発泡倍率が10〜33倍と低いときは、肉厚が80
%減じるように型内ビーズ発泡成形品を圧縮すると、ス
チレン系樹脂発泡成形品に亀裂が生じてしまう。
(Ii). The density of bead foam molded products in the mold is 11.6g / or 16.8
g / like foaming ratio of 60 to 100 times and high foaming,
It can be compressed until the thickness of the foamed bead in the mold is reduced by 80%, but the density of the foamed bead in the mold is 30 ~
When the foaming ratio is as low as 10 to 33 times with 100 g /, the wall thickness is 80
When the in-mold bead foam molded product is compressed so as to reduce the percentage, the styrene resin foam molded product is cracked.

従つて、圧縮の程度を漸時、低い方から高い方へと段
階を経て行わなければ高弾性の発泡成形品を得ることが
できない。
Therefore, unless the degree of compression is gradually and gradually increased from low to high, a highly elastic foam molded article cannot be obtained.

本発明は、高発泡倍率の型内ビーズ発泡成形品はもち
ろん、低発泡倍率の型内ビーズ発泡成形品でも、押出発
泡成形品であつても高圧縮することにより極めて短時間
に、割れのない高弾性の樹脂発泡成形品を製造する方法
を提供する。
The present invention is not limited to the in-mold bead foam molded product having a high expansion ratio, the in-mold bead foam molded product having a low expansion ratio, and the extruded foam molded product can be cracked in a very short time by high compression. Provided is a method for producing a resin foam molded article having high elasticity.

(課題を解決する具体的手段) 本発明においては、独立気泡構造(50%以上の気泡が
独立気泡であればよい)の熱可塑性樹脂発泡成形品を減
圧処理した後、圧縮することにより極めて短時間に高弾
性の発泡成形品とすることができる。
(Specific Means for Solving the Problems) In the present invention, a thermoplastic resin foam molded article having a closed cell structure (50% or more of the cells only need to be closed cells) is subjected to a reduced pressure treatment and then compressed to be extremely short. A foamed article having high elasticity can be obtained in a short time.

(樹脂発泡成形品) 発泡成形品は、型内ビーズ発泡成形品、圧縮充填型内
ビーズ融着成形品、押出発泡品、射出発泡品等成形法を
問わず、独立気泡率が50%以上、好ましくは65〜98%以
上のポリスチレン、ABS、スチレン・α−メチルスチレ
ン・メタクリル酸メチル共重合体、スチレン・アクリロ
ニトリル共重合体等のスチレン系樹脂;ポリプロピレ
ン、ポリエチレン、エチレン・酢酸ビニル共重合体、ポ
リアミド、ポリ塩化ビニル、尿素樹脂等の熱可塑性樹脂
の発泡体が使用できる。これらは、ブロツク状の発泡成
形品を電熱線で切断したものであつてもよい。更に、架
橋されていてもよい。
(Resin foam molded products) Foam molded products have a closed cell ratio of 50% or more, regardless of the molding method, such as in-mold bead foam molded products, compression-filled bead fusion molded products, extruded foam products, injection foamed products, etc. Preferably 65-98% or more polystyrene, ABS, styrene-based resin such as styrene-α-methylstyrene-methyl methacrylate copolymer, styrene-acrylonitrile copolymer; polypropylene, polyethylene, ethylene-vinyl acetate copolymer, A foam of a thermoplastic resin such as polyamide, polyvinyl chloride, and urea resin can be used. These may be obtained by cutting a block-shaped foam molded product with a heating wire. Further, it may be crosslinked.

発泡成形品の密度は、5〜100g/、好ましくは8〜3
0g/である。密度が小さい程、高弾性を示す成形品を
得ることができる。
The density of the foam molded article is 5 to 100 g /, preferably 8 to 3 g.
0 g /. As the density is smaller, a molded product having higher elasticity can be obtained.

(減圧処理) 発泡成形機の減圧処理は第1図に示す減圧室2に発泡
成形品1を入れ、減圧室内を−760mmHg〜−400mmHg、好
ましくは−760mmHg〜700mmHgの減圧度にまで真空ポンプ
5を用いて減圧し、発泡成形品内部のセルの減圧度を−
759mmHg〜−250mmHgとする。
(Decompression treatment) In the decompression treatment of the foam molding machine, the foam molded article 1 is placed in the decompression chamber 2 shown in FIG. And reduce the degree of decompression of the cells inside the foamed molded article to −
759 mmHg to -250 mmHg.

容積の大きい減圧室を使用すると一度に多くの発泡成
形品を減圧処理することができる。勿論、減圧室を備え
させたプレス金型を用い、減圧処理、その後に続く圧縮
を行つてもよいが、その時は減圧処理が成形工程におけ
る律速段階となり発泡成形品の生産性が向上しない。
When a vacuum chamber having a large volume is used, many foam molded articles can be subjected to vacuum treatment at one time. Of course, a press mold provided with a decompression chamber may be used to perform the decompression process and the subsequent compression. However, in this case, the decompression process is the rate-determining step in the molding process, and the productivity of the foam molded article is not improved.

(圧縮処理) 減圧処理がなされた発泡成形品を、減圧室より取り出
し、直ちに、又は、大気圧下に0.5〜10時間放置し、発
泡成形品のセル内圧が、−150mmHg〜−750mmHg、好まし
くは−700mmHg〜−230mmHgとなつたものをプレス成形機
(3,3′)を用いて圧縮前の成形品の肉厚(t0)の40〜9
0%(圧縮後の成形品の肉厚t1は0.6t0〜0.1t0)圧縮す
る。圧縮する速度は特に限定しないが好ましくは50〜60
0mm/分程度がよい。圧縮時の温度は常温でも、樹脂の軟
化点より20℃低い位の温度まで加熱してもよい。また圧
縮の回数は1回でも数回でもよい。
(Compression treatment) The foam molded product subjected to the decompression treatment is taken out of the decompression chamber, and is immediately or left for 0.5 to 10 hours under the atmospheric pressure, and the internal pressure of the foam molded product is from -150 mmHg to -750 mmHg, preferably -700mmHg~-230mmHg and the summer was that the press molding machine (3, 3 ') the wall thickness of the molded article before compression by using the (t 0) 40~9
0% (thickness t 1 of the molded article after compression 0.6t 0 ~0.1t 0) compresses. The compression speed is not particularly limited, but is preferably 50 to 60.
About 0mm / min is good. The temperature at the time of compression may be room temperature or may be heated to a temperature lower by 20 ° C. than the softening point of the resin. The number of compressions may be one or several.

この時、型枠4はあつても(第3図)、なくても(第
2図)よい。
At this time, the mold 4 may be provided (FIG. 3) or not (FIG. 2).

圧縮処理され、プレスより解放された発泡成形品の肉
厚t2は圧縮される前の肉厚t0の50〜90%(0.5t0〜0.9
t0)となるように圧縮を行なう。
Is compressed, 50-90% of the wall thickness t 0 of the previous thickness t 2 of the released molded foam from the press to be compressed (0.5 t 0 to 0.9
t 0 ).

更に、発泡成形品1をプレス機により圧縮荷重を一方
向のみで圧縮して発泡成形品とした場合、圧縮荷重をか
けた方向の両面の歪はでないものの、圧縮荷重をかけな
い面の歪が若干生じるため、使用する用途によつて第3
図に示すように発泡成形品ブロツクの三方向に圧縮荷重
をかければ歪が解消され、三方向とも高弾性を示し、切
削加工が容易となり、また、緩衝材としてダンボール箱
と冷蔵庫やテレビ等の収納物品のすき間に詰める場合、
三次元方向に変形させることができるので緩衝材の挿入
が容易となる利点を有する。
Further, when the foamed molded product 1 is compressed into a foamed molded product by compressing the compression load in only one direction by a press machine, although the distortion on both surfaces in the direction in which the compression load is applied is not, the distortion on the surface not subjected to the compression load is reduced. Due to slight occurrence, third
As shown in the figure, if a compressive load is applied in three directions of the foam molded product block, the distortion is eliminated, high elasticity is exhibited in all three directions, cutting becomes easy, and a cardboard box and a refrigerator or TV as a cushioning material are used. When filling in the gaps of stored items,
Since it can be deformed in a three-dimensional direction, there is an advantage that it becomes easy to insert the cushioning material.

(作用効果) 本発明によれば発泡成形品を減圧処理してから圧縮す
るので、低発泡倍率の発泡成形品でも一回の圧縮のみ
で、高弾性の発泡成形品とすることができる。
(Effects) According to the present invention, since the foam molded article is compressed after being subjected to a reduced pressure treatment, a foam molded article having a low expansion ratio can be made into a highly elastic foam molded article by only one compression.

(実施例等) 実施例1〜6 独立気泡率が90%、密度が12g/のポリスチレン型内
ビーズ発泡成形品ブロツク(縦1840mm×横930mm×高さ4
25mm)をニクロム線で切断して300mm×300mm×150mmの
寸法の直方体ブロツクとした。
(Examples, etc.) Examples 1 to 6 A block of a bead foam molded product in a polystyrene mold having a closed cell ratio of 90% and a density of 12 g / (length 1840 mm × width 930 mm × height 4
25mm) was cut with a nichrome wire to form a rectangular parallelepiped block measuring 300 mm x 300 mm x 150 mm.

この寸法のブロツク、5個を内容積が100の減圧室
内に入れ、ついで減圧室を−750mmHgまで減圧した後、
0.5〜20時間減圧室内に保存した。
After placing five blocks of this size in a decompression chamber with an internal volume of 100, and then depressurizing the decompression chamber to -750 mmHg,
Stored in a vacuum chamber for 0.5-20 hours.

ついで、この減圧処理したブロツクを減圧室より取り
出し、直ちに、又は大気圧下に放置した後、10トンプレ
スで高さ方向に500mm/分の速度でその肉厚が30mm(圧縮
率80%)となるように圧縮し、ついでプレスを上昇させ
て高弾性の発泡体を得た。
Then, the block subjected to the decompression treatment is taken out of the decompression chamber, and immediately or after being left under the atmospheric pressure, the thickness is reduced to 30 mm (compression rate 80%) at a speed of 500 mm / min in a height direction by a 10-ton press. And then the press was raised to obtain a highly elastic foam.

この高弾性発泡体の割れの有無、圧縮弾性率(JIS
K−7220)、を表1に示す。
The presence or absence of cracks in this highly elastic foam, the compression modulus (JIS
K-7220) are shown in Table 1.

実施例7 減圧処理時の圧力を−759mmHgとする他は実施例1と
同様にして表1に示す物性の弾性発泡体を得た。
Example 7 An elastic foam having the physical properties shown in Table 1 was obtained in the same manner as in Example 1 except that the pressure during the depressurizing treatment was -759 mmHg.

比較例1 減圧処理を行わない他は、実施例1と同様にしてプレ
スしたところ、発泡成形体は破損した。又、圧縮弾性率
も減圧処理を行つたものと較べて2倍以上であつた。
Comparative Example 1 Except not performing the decompression treatment, the foamed molded product was broken when pressed in the same manner as in Example 1. Further, the compression modulus was more than twice as high as that obtained by performing the decompression treatment.

実施例8〜12 独立気泡率が95%、密度が17g/のポリスチレン型内
ビーズ発泡成形品ブロツク(縦1840mm×横930mm×高さ4
25mm)をニクロム線で切断して300mm×300mm×150mmの
寸法の直方体ブロツクとした。
Examples 8 to 12 Blocks of foamed beads in a polystyrene mold having a closed cell ratio of 95% and a density of 17 g / (length 1840 mm × width 930 mm × height 4
25mm) was cut with a nichrome wire to form a rectangular parallelepiped block measuring 300 mm x 300 mm x 150 mm.

この寸法のブロツクを減圧室内に入れ、ついで減圧室
を−755mmHgまで減圧した状態で3時間保存した発泡成
形品のセル内圧は−230mmHgであつた。ついでこの減圧
処理したブロツクを減圧室より取り出した後、10トンプ
レスで高さ方向に200mm/分の速度で圧縮率が40%、50
%、60%、70%および80%となるように圧縮し、ついで
プレスを上昇させて高弾性の発泡体を得た。
A block of this size was placed in a decompression chamber, and then the pressure inside the decompression chamber was reduced to -755 mmHg for 3 hours, and the foamed molded product had an internal cell pressure of -230 mmHg. Then, the block subjected to the decompression treatment was taken out of the decompression chamber, and the compression ratio was 40%, 50% in the height direction at a speed of 200 mm / min by a 10-ton press.
%, 60%, 70% and 80% and then the press was raised to obtain a highly elastic foam.

この高弾性発泡体の圧縮弾性率、高さを表2に示す。 Table 2 shows the compression elastic modulus and height of this high elastic foam.

比較例2、3 圧縮率を20%および30%とする他は実施例6〜10と同
様にして表2に示す物性の発泡成形品を得た。
Comparative Examples 2 and 3 A foam molded article having the physical properties shown in Table 2 was obtained in the same manner as in Examples 6 to 10, except that the compression ratio was changed to 20% and 30%.

比較例4 減圧処理を行わない他は実施例9と同様にして表2に
示す物性の発泡成形品を得た。
Comparative Example 4 A foam molded article having the physical properties shown in Table 2 was obtained in the same manner as in Example 9 except that the decompression treatment was not performed.

実施例13 実施例1において、高さ方向に圧縮後、横方向、縦方
向にもそれぞれ瞬時に80%圧縮して得た三方向圧縮処理
発泡体の各方向の圧縮弾性率、寸法は次の通りであつ
た。
Example 13 In Example 1, the compression elastic modulus and dimensions in each direction of the three-way compression-treated foam obtained by instantaneously compressing 80% each in the horizontal and vertical directions after compression in the height direction are as follows. It was on the street.

実施例14 密度が10.8g/、独立気泡率が82%のポリスチレン型
内ビーズ発泡成形体のニクロム線切断ブロツク(縦300m
m×横300mm×高さ150mm)を減圧室で−755mmHg、10時間
の条件下で減圧処理した後、5分後にその高さ方向に80
%圧縮して表3に示す物性の弾性発泡体ブロツクを得
た。
Example 14 A nichrome wire cutting block of a foamed bead in a polystyrene mold having a density of 10.8 g / and a closed cell ratio of 82% (length: 300 m)
m × 300 mm × 150 mm) in a vacuum chamber at −755 mmHg for 10 hours, and after 5 minutes 80
% To obtain an elastic foam block having the physical properties shown in Table 3.

比較例5〜6 実施例13において、減圧処理を施こさない他は同様に
して(比較例5)または、減圧処理を施こさないで、圧
縮を3回繰り返した(比較例6)他は同様にして表3に
示す物性の弾性ブロツクを得た。
Comparative Examples 5 to 6 In Example 13, the procedure was the same except that the decompression treatment was not performed (Comparative Example 5), or the compression was repeated three times without the decompression treatment (Comparative Example 6), except that Thus, an elastic block having the physical properties shown in Table 3 was obtained.

実施例15 型内ビーズ発泡成形した密度が15g/、独立気泡率が
86%のポリスチレン発泡体(300mm×300mm×150mm)を
キヤビテイ内に内蔵する型のチヤンバーを−500mmHgに
減圧し、30分間その圧を保つことによりチヤンバーにス
チーム孔で連通するキヤビテイ内も同圧に減圧して発泡
体を減圧処理した後、上金型を更に下降して発泡体を40
%圧縮し、ついで型を開いて曲げ弾性率が9.8kg/cm2
高さ98mmの割れのない発泡体を得た。
Example 15 In-mold bead foam molding was performed at a density of 15 g / closed cell rate.
A chamber containing 86% polystyrene foam (300 mm x 300 mm x 150 mm) inside the cavity is depressurized to -500 mmHg and maintained at that pressure for 30 minutes to maintain the same pressure inside the cavity that communicates with the chamber via a steam hole. After decompressing the foam and depressurizing the foam, the upper mold is further lowered to reduce the foam to 40
% Compression, then open the mold and have a flexural modulus of 9.8 kg / cm 2 ,
A crack-free foam having a height of 98 mm was obtained.

実施例16 型内ビーズ成形した密度が50g/、圧縮弾性率が70.7
kg/cm2、独立気泡率が約86%のポリプロピレン系樹脂発
泡体を減圧室で−500mmHgで180分間減圧処理した後、こ
れを減圧室より取り出し、これをプレス金型で上下方向
に80%、三回圧縮して得たものの圧縮弾性率は15.0kg/c
m2であつた。
Example 16 The density of beads formed in a mold was 50 g /, and the compression modulus was 70.7.
A polypropylene resin foam having a closed cell ratio of about 86% in kg / cm 2 is subjected to a decompression treatment at −500 mmHg for 180 minutes in a decompression chamber, and then taken out of the decompression chamber, and is taken up and down by 80% in a pressing mold. The compression modulus of the product obtained by compressing three times is 15.0 kg / c
Atsuta in m 2.

比較例7 実施例16において、減圧処理しない他は同様にして得
た圧縮処理成形体の圧縮弾性率は26.0kg/cm2であつた。
Comparative Example 7 A compression-treated molded article obtained in the same manner as in Example 16 except that the depressurization treatment was not performed was 26.0 kg / cm 2 .

実施例17 実施例16において、80%圧縮率で3回の圧縮処理を上
下方向、前後方向、左右方向に行つたものの圧縮弾性率
は約17〜18kg/cm2であつた。
Example 17 In Example 16, three compression treatments at 80% compression rate were performed in the up-down direction, the front-rear direction, and the left-right direction, but the compression elastic modulus was about 17 to 18 kg / cm 2 .

比較例8 実施例17において、減圧処理を行わない他は同様に圧
縮処理して得たものの圧縮弾性率は35〜38kg/cm2であつ
た。
Comparative Example 8 In Example 17, except that the decompression treatment was not performed, the same compression treatment was performed, but the compression elastic modulus was 35 to 38 kg / cm 2 .

【図面の簡単な説明】[Brief description of the drawings]

第1図は発泡成形品を減圧している状態を示す断面図、
第2図と第3図は発泡成形品を圧縮している状態を示す
平面図、第4図は発泡成形品を圧縮する方向を示す斜視
図である。
FIG. 1 is a cross-sectional view showing a state where the pressure of a foam molded article is reduced;
2 and 3 are plan views showing a state in which the foam molded article is compressed, and FIG. 4 is a perspective view showing a direction in which the foam molded article is compressed.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】独立気泡構造の熱可塑性樹脂発泡成形体を
減圧室に入れ、減圧下に晒した後、次いでこの発泡成形
体をその厚みの40〜90%まで圧縮することを特徴とする
高弾性の熱可塑性樹脂発泡成形品の製造方法。
1. A foamed thermoplastic resin article having a closed cell structure is placed in a reduced pressure chamber, exposed to a reduced pressure, and then the foamed article is compressed to 40 to 90% of its thickness. A method for producing an elastic thermoplastic resin foam molded article.
【請求項2】独立気泡構造の熱可塑性樹脂発泡成形体ブ
ロツクを減圧室に入れ、減圧下に晒した後、次いでこの
発泡成形体ブロツクを上下面、前後面、左右面ともその
寸法の40〜90%まで圧縮することを特徴とする高弾性の
熱可塑性樹脂発泡成形体ブロツクの製造方法。
2. A block of a thermoplastic resin foam molded article having a closed cell structure is placed in a reduced pressure chamber and exposed to a reduced pressure. A method for producing a highly elastic thermoplastic resin foam block, wherein the block is compressed to 90%.
JP12087589A 1989-05-15 1989-05-15 Method for producing highly elastic thermoplastic resin foam molded article Expired - Fee Related JP2774814B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12087589A JP2774814B2 (en) 1989-05-15 1989-05-15 Method for producing highly elastic thermoplastic resin foam molded article

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12087589A JP2774814B2 (en) 1989-05-15 1989-05-15 Method for producing highly elastic thermoplastic resin foam molded article

Publications (2)

Publication Number Publication Date
JPH02299821A JPH02299821A (en) 1990-12-12
JP2774814B2 true JP2774814B2 (en) 1998-07-09

Family

ID=14797120

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12087589A Expired - Fee Related JP2774814B2 (en) 1989-05-15 1989-05-15 Method for producing highly elastic thermoplastic resin foam molded article

Country Status (1)

Country Link
JP (1) JP2774814B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10132494A1 (en) * 2001-07-05 2003-02-06 Dmt Gmbh Feinwerktechnische Ko Process for treating foam particles in pourable form and device for carrying out the process

Also Published As

Publication number Publication date
JPH02299821A (en) 1990-12-12

Similar Documents

Publication Publication Date Title
NO20002202L (en) Cast polyolefin and polypheny oxide products and process for their preparation
CA2953201A1 (en) Pressure-dependent foam moulding of poly(meth)acrylimide particles in closed moulds for producing rigid foam cores
JP2774814B2 (en) Method for producing highly elastic thermoplastic resin foam molded article
JPH0138660B2 (en)
EP0288634B1 (en) A process for producing mouldings from an expanded styrene polymer
JPS6134378B2 (en)
EP0317995A3 (en) Process for preparing foamed article from propylene resin
JPH09254179A (en) Foamed synthetic resin molded object and its molding method
JP2012201820A (en) Expansion-molded product and production method therefor
JPS60190335A (en) Manufacture of expanded resin molding
JPH0114014B2 (en)
KR101967367B1 (en) Manufacturing method for sound proof plate using styrofoam
JPH0622921B2 (en) Method for manufacturing foamed resin molded product
SU1199768A1 (en) Method of producing foam polystyrene
JPH02150335A (en) Manufacture of molding within expansion resin die
EP0537192A1 (en) Method of forming thermoplastic materials
US20240017451A1 (en) Method for manufacturing laminate
JPS5849384B2 (en) Manufacturing method of ethylene resin foam molded product
JP6391346B2 (en) Polystyrene resin foam
RU2179511C1 (en) Amber article manufacture method
JPH0622920B2 (en) Method for manufacturing thermoplastic resin in-mold foam molding
JPH0698695B2 (en) Foam molding method for thermoplastic synthetic resin block
JPH0813478B2 (en) Method for producing polystyrene resin foam molded article with skin
JPH09164585A (en) Forming method of thermoplastic resin foam sheet
JP3485357B2 (en) Method for producing hollow molded article filled with expanded beads

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees