JPH037318A - Foamable thermoplastic resin and manufacture thereof - Google Patents
Foamable thermoplastic resin and manufacture thereofInfo
- Publication number
- JPH037318A JPH037318A JP1141493A JP14149389A JPH037318A JP H037318 A JPH037318 A JP H037318A JP 1141493 A JP1141493 A JP 1141493A JP 14149389 A JP14149389 A JP 14149389A JP H037318 A JPH037318 A JP H037318A
- Authority
- JP
- Japan
- Prior art keywords
- thermoplastic resin
- foam
- shape
- cut
- loose
- 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
Links
Landscapes
- Buffer Packaging (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
任意形状の被包装物を段ボール箱など定形梱包体に収納
する場合、被包装物と梱包体の間に隙間が生じて安定性
が悪く、輸送時には被包装物を損傷する。これらを防止
するため、熱可塑性樹脂発泡体等の小片からなるいわゆ
るバラ状M1体を隙間に詰める包装形態がひろく採用さ
れている。[Detailed Description of the Invention] (Industrial Application Field) When a packaged object of an arbitrary shape is housed in a regular package such as a cardboard box, a gap is created between the packaged object and the package, resulting in poor stability. The packaged items will be damaged during transportation. In order to prevent these problems, a packaging form in which so-called loose M1 bodies made of small pieces of thermoplastic resin foam or the like are stuffed into the gaps has been widely adopted.
本発明は熱可塑性樹脂発泡体よりなるバラ状緩衝体に関
L、特に従来品の形状と異なる三次元的に湾曲したバラ
状緩衝体及びその製造方法に関する。The present invention relates to a bulk cushioning body made of thermoplastic resin foam, and more particularly to a three-dimensionally curved bulk cushioning body different from the shape of conventional products, and a method for manufacturing the same.
(従来の技術)
従来のバラ状緩衝体には、特公昭42−4512号公報
に開示されている断面円形の短繊維構造の三次元的湾曲
をもつ紐状の形状、特開昭59−187566号公報に
開示されている異形断面をもつ紐状の形状、あるいは特
公昭47−30102号公報、実公昭57−58141
号公報に開示されている比較的三次元的湾曲の少ない形
状などが知られている。(Prior Art) Conventional loose shock absorbers include a three-dimensionally curved string-like shape having a short fiber structure with a circular cross section as disclosed in Japanese Patent Publication No. 42-4512, and Japanese Patent Application Laid-Open No. 59-187566. The string-like shape with an irregular cross section disclosed in Japanese Patent Publication No. 47-30102, Japanese Utility Model Publication No. 57-58141
A shape with relatively little three-dimensional curvature is known, as disclosed in Japanese Patent Publication No.
(発明が解決しようとする問題点)
従来技術の湾曲した紐状のバラ状緩衝体は、使用前に既
に緩衝体が個々に互いに絡み合っているので、次のよう
な不都合があった。つまり使用時、紙箱などの収納容器
の壁と被包装物品との間の空間間隙が狭い場合には、こ
の狭い間隙金詰めるために大きく絡み合った紐状[51
体同志を小分けするのに手間がかかった。又、絡み合い
を解くために力をかけて引張ると紐は破断し短くなり、
その結果として紐の湾曲が小さくなり三次元的充填効果
が少なくなった。(Problems to be Solved by the Invention) The curved string-like loose cushioning bodies of the prior art have the following disadvantages because the cushioning bodies are individually entangled with each other before use. In other words, during use, if the space gap between the wall of the storage container such as a paper box and the packaged item is narrow, large intertwined strings [51
It took a lot of effort to separate the body comrades into smaller parts. Also, if you apply force and pull to untangle the string, it will break and become shorter.
As a result, the curvature of the string was reduced and the three-dimensional filling effect was reduced.
特公昭47−30102号公報、実公昭57−5814
1号公報に開示された別の従来技術のバラ状緩衝体は、
緩衝体個々の絡み合いは少なく、紐状緩衝体と比較する
と作業上の取り汲いは容易である。しかしながらその反
面、必然的に使用時紙箱など収納容器への充填量が多く
なるという不経済性がある。更に、包装箱の移動時、荷
動きにより緩衝体が動きやすく被包装物品に対する緩衝
効果が減少するという欠陥があった。Special Publication No. 47-30102, Publication No. 57-5814
Another conventional loose buffer body disclosed in Publication No. 1 is as follows:
There is less entanglement between the individual cushioning bodies, and compared to string-like cushioning bodies, handling is easier. However, on the other hand, it is uneconomical that the amount of filling into a storage container such as a paper box inevitably increases during use. Furthermore, when the packaging box is moved, the cushioning body tends to move due to the movement of the cargo, reducing the cushioning effect on the packaged articles.
更に従来の熱可塑性樹脂発泡体のバラ状y1衝体の製造
においては、通常特公昭47−30102号公報、特開
昭59−187566号公報に開示されているように、
押出機の先端に付設した多数個の小径押出孔を有する口
金より、発泡剤を含有する溶融熱可塑性樹脂を大気中に
押出L、発泡を阻止するためにこの押出物を直ちに冷却
水中に導き急冷し40℃以下に冷却したのち、所定長さ
に細断して、−旦発泡性ペレットとなL、しかるのちこ
の発泡性ベレットを高温スチームなどで再加熱して再発
泡させ製品を得るというように、水中などでの急冷工程
を必要とし製造上わづられしく、かつ不経済な工程を要
するという欠陥があった。Furthermore, in the production of conventional bulk Y1 blocks of thermoplastic resin foam, as disclosed in Japanese Patent Publication No. 47-30102 and Japanese Patent Application Laid-Open No. 59-187566,
A molten thermoplastic resin containing a foaming agent is extruded into the atmosphere through a nozzle with a large number of small-diameter extrusion holes attached to the tip of the extruder, and the extrudate is immediately introduced into cooling water for rapid cooling to prevent foaming. After cooling to below 40°C, it is shredded into a predetermined length and turned into expandable pellets.Then, the expandable pellets are reheated with high-temperature steam to re-foam and obtain a product. However, there was a drawback in that it required a rapid cooling process in water, which was a difficult and uneconomical process to manufacture.
本発明は上記問題点を一挙に解決するためになされたも
ので、その目的は(イ)三次元的湾曲が大きく、かつバ
ラ状MWk体相互の絡み合いが少なく、包装時の作業性
がよい、 (ロ)充填効率が大きい、すなわち包装時充
填使用量が少なく、かつ十分な緩衝機能を示し荷動きが
少ない、 (ハ)製造が容易で経済的に広い範囲で使用
し得る。The present invention has been made to solve the above problems all at once, and its purpose is (a) to have a large three-dimensional curvature, less entanglement of loose MWk bodies with each other, and good workability during packaging; (b) It has a high filling efficiency, that is, the amount of filling used during packaging is small, and it has a sufficient buffering function, resulting in less cargo movement. (c) It is easy to manufacture and can be economically used in a wide range of areas.
本発明はこれらの特性を満たすことができる改良された
熱可塑性樹脂発泡体とその製造方法を提供する。The present invention provides an improved thermoplastic resin foam that can meet these properties and a method for producing the same.
(問題を解決するための手段) 発明の内容を図面を用いて詳述する。(Means to solve the problem) The content of the invention will be explained in detail using drawings.
本発明の熱可塑性樹脂発泡体は、密度=領 005〜0
.05g/mLで、第1図、第2図、第3図に示すごと
く三次元的に湾曲した形状を持つもので、第1図a、第
2図5 第3図はバラ状緩衝体の横方向面を水平方向よ
りみたスケッチ図で、TIは中央部肉厚、T2は湾曲し
た先端部肉厚、Yは湾曲度を示す全体幅、しはバラ状M
衝体の長さで、第1図すにおいてWは上面よりみたバラ
状榎W体の成形幅を示す。The thermoplastic resin foam of the present invention has a density=range of 005 to 0.
.. 05g/mL, and has a three-dimensionally curved shape as shown in Figures 1, 2, and 3. This is a sketch diagram of the direction plane viewed from the horizontal direction, where TI is the thickness at the center, T2 is the thickness at the curved tip, Y is the overall width indicating the degree of curvature, and shi is the loose shape M.
In Fig. 1, W indicates the molding width of the rose-shaped Enoki W body when viewed from the top surface.
長さしの実寸法は30〜100關であり、TI/し=0
.1〜0.6、W/L=0. 2〜領 5、Y/L=0
. 4〜1. 5、 Y/W=1. 2〜5゜0、T
+ / T 2 > 2を満たす寸法を有する形状を
示すことで、上記の本発明の目的を達成することを特徴
とする。The actual length is 30 to 100 degrees, and TI/SI = 0
.. 1-0.6, W/L=0. 2~Region 5, Y/L=0
.. 4-1. 5, Y/W=1. 2~5゜0, T
The present invention is characterized in that the object of the present invention described above is achieved by exhibiting a shape having dimensions that satisfy +/T 2 > 2.
上記特性値において、発泡体の密度が0.05g /
m 2以上では発泡体は硬すぎ、被包装物品にすり傷を
つける恐れがあるばかりでなく後述する充填効率が小さ
く使用量が多くなり不経済であり、i度が0.005g
/mu以下ではバラ状緩衝体の強度、弾性などが低下L
、[衝性も低下する欠点が生じてくる。In the above characteristic values, the density of the foam is 0.05g/
m2 or more, the foam is too hard and may cause scratches on the packaged goods, and the filling efficiency, which will be described later, is low and the amount used is large, making it uneconomical.
/mu or less, the strength, elasticity, etc. of the bulk shock absorber decreases L
, [A drawback arises in that the impact resistance also decreases.
Lが3’ O1m以下では箱などの収納容器と被包装物
品との間の空間間隙にバラ状M衝体を詰める場合小さす
ぎて充填効率が悪く不経済であり、100闘以上では包
装物品の移動時に荷動きが起こつやすく、又yI衝効果
が低下するという欠点が生じやすい。If L is less than 3'O1m, it will be too small to fill the gap between the storage container such as a box and the packaged item with loose M blocks, resulting in poor filling efficiency and uneconomical conditions; The disadvantage is that cargo movement tends to occur during transportation, and that the yI impact effect is reduced.
TI/Lが0. 1以下ではバラ状M1体は折れ易くな
り、0゜6以上では湾曲が少なくなり充填効率が低下す
る。TI/L is 0. If it is less than 1, the loose M1 body will break easily, and if it is more than 0°6, the curvature will decrease and the filling efficiency will decrease.
TI/T2が2以下では湾曲の大きなバラ状緩衝体は得
にくく、したがって充填効率の大きな物は得られない欠
点が生じてくる。When TI/T2 is less than 2, it is difficult to obtain a bulky buffer with a large degree of curvature, resulting in the disadvantage that a product with a high filling efficiency cannot be obtained.
W/Lが0.2以下ではバラ状#1iWr体は折れ易く
なり、0.5以上では荷動きが生じやすく、かつ充填効
率が低下するという欠点が生じてくる。If W/L is less than 0.2, the loose #1iWr body is likely to break, and if it is greater than 0.5, there will be disadvantages in that cargo movement is likely to occur and filling efficiency is reduced.
Y / Lが0. 4以下でも、1. 5以上でも、充
填効率が極端に低下し使用上不経済であり、Y/Wが1
.2以下では被包装物品の荷動きが生じやすく、50以
上ではバラ状111体相互の絡み合いが起こりやすくな
る欠点が生じてくる。Y/L is 0. Even if it is 4 or less, 1. If it is more than 5, the filling efficiency will be extremely reduced and it will be uneconomical to use, and if Y/W is 1.
.. If the number is less than 2, the goods to be packaged tend to move, and if it is more than 50, the loose 111 pieces tend to get entangled with each other.
本発明は以上の状況を詳細に試験した結果、上記特性値
の範囲に限定した形状にすることにより、発明の目的と
する改良されたバラ状緩衝体を提供するに至ったもので
ある。As a result of detailed tests on the above-mentioned situation, the present invention has been able to provide an improved bulk shock absorbing body, which is the object of the present invention, by making the shape limited to the range of the above-mentioned characteristic values.
上述の本発明のバラ状y1衝体の製造方法は、押出機先
端に付設した第7図、第8図、第9図に示すごとき半円
形、円形、四角形又は楕円形、半楕円形その他の開口形
状の複数の細孔を有する口金より、発泡剤を含有する溶
融熱可塑性樹脂を大気中に押出し発泡成形体を得る熱可
塑性樹脂発泡体の製造方法において、これらの押出し細
孔より押出L、発泡せしめて得られた熱可塑・性樹脂発
泡体細条を、冷却後押出方向に対して第4〜6図aに示
すごとく角度θ度をもつように斜めに切断L、ついで切
断した発泡体細条を加熱し再発泡せしめ上記のT7、T
2、Y、W、Lが所定の寸法を満たすような三次元的に
湾曲した形状の本発明のバラ状緩衝体を得ることを特徴
とする。The above-described method for producing the bulk Y1 blanks of the present invention can be carried out using a semicircular, circular, square, elliptical, semi-elliptical or other shape as shown in FIGS. 7, 8 and 9 attached to the tip of the extruder. In a method for producing a thermoplastic resin foam, in which a molten thermoplastic resin containing a blowing agent is extruded into the atmosphere through a die having a plurality of open-shaped pores to obtain a foam molded article, extrusion L through these extrusion pores, After cooling, the thermoplastic resin foam strips obtained by foaming are cut diagonally at an angle of θ degrees with respect to the extrusion direction as shown in FIGS. 4 to 6 a, and the cut foam is then cut. The strips are heated and re-foamed to T7 and T above.
2. The present invention is characterized in that it obtains a loose shock absorber of the present invention having a three-dimensionally curved shape such that Y, W, and L satisfy predetermined dimensions.
本発明において、熱可塑性樹脂とは、ポリスチレン樹脂
、スチレン成分が主体で、他のスチレンと共重合し得る
不飽和有機化合物との共重合体であるポリスチレン系樹
脂、エチレン、プロピレン、ブテンなどのポリオレフィ
ン樹脂、エチレン、プロピレン、ブテンなどを主成分と
するポリオレフィン系樹脂、ポリメチルメタアクリレー
トなどのアクリル系樹脂、ポリ塩化ビニール系樹脂、ポ
リアミド系樹脂などである。In the present invention, thermoplastic resins include polystyrene resins, polystyrene resins that are mainly composed of styrene components and copolymers with unsaturated organic compounds that can be copolymerized with other styrene, and polyolefins such as ethylene, propylene, and butene. These include resins, polyolefin resins whose main components are ethylene, propylene, butene, etc., acrylic resins such as polymethyl methacrylate, polyvinyl chloride resins, and polyamide resins.
これらの樹脂に混合L、発泡体となすための発泡剤とし
ては、例えばプロパン、ブタン、ペンタンなどの低沸点
炭化水素、メチルクロライド、メチレンクロライド、モ
ノクロロジフルオロメタン、ジクロロモノフルオロメタ
ン、ジクロロジフルオロメタン、トリクロロモノフルオ
ロメタン、ジクロロテトラフルオロエタンなどのハロゲ
ン化炭化水素などの単品あるいはこれらの混合物、及び
これらと炭酸ガス、窒素などの無機系ガスとの混合物が
有効である。これら低沸点発泡剤の添加量は所望する発
泡体の密度によって異なるが、前述の熱可塑性樹脂10
0部に対して3〜30部が好ましい。When mixed with these resins, blowing agents for forming foams include, for example, low-boiling hydrocarbons such as propane, butane, and pentane, methyl chloride, methylene chloride, monochlorodifluoromethane, dichloromonofluoromethane, dichlorodifluoromethane, Single or mixtures of halogenated hydrocarbons such as trichloromonofluoromethane and dichlorotetrafluoroethane, and mixtures of these with inorganic gases such as carbon dioxide and nitrogen are effective. The amount of these low boiling point blowing agents added varies depending on the density of the desired foam, but the amount of the above-mentioned thermoplastic resin 10
It is preferably 3 to 30 parts relative to 0 parts.
また発泡体の気泡径を調整するための気泡fill整剤
としてはタルク、炭酸カルシウム、アルミナなどの無機
質の微粉体、ステアリン酸カルシウム、ステアリン酸亜
鉛などの金属石鹸類の微粉体、重曹とクエン酸などの混
合物が使用される。これら気泡!ll整剤の添加量は前
述の熱可塑性樹脂100部に対して0. 1〜3.0部
が好ましい。In addition, foam fill agents for adjusting the cell diameter of the foam include fine inorganic powders such as talc, calcium carbonate, and alumina, fine powders of metal soaps such as calcium stearate and zinc stearate, baking soda and citric acid, etc. A mixture of is used. These bubbles! The amount of additive added is 0.0 parts per 100 parts of the above-mentioned thermoplastic resin. 1 to 3.0 parts is preferred.
更に必要に応じて着色剤、帯電防止剤、可塑削なとも熱
可塑性樹脂に添加し得る。Furthermore, colorants, antistatic agents, and plasticizing agents may be added to the thermoplastic resin as necessary.
(作用)
本発明の熱可塑性樹脂発泡体のバラ状緩衝体及びその製
造において、これらの成分を混合し押出し発泡させるに
は、通常スクリュータイプの押出機が使用される。即ち
熱可塑性樹脂と気泡調整剤などを押出機に供給L、これ
を熱可塑性樹脂の軟化温度以上の温度に加熱し1回転す
るスクリューにより混練し溶融可塑化したあと、この溶
融樹脂中に、高圧ポンプにより押出機のベント孔などよ
り低沸点発泡剤を圧入L、更に混練して発泡剤を溶融熱
可塑性樹脂中に均一に分散させたのち、所定温度までこ
の溶融熱可塑性樹脂組成物を冷却L、しかるのちに押出
機先端に付設した多数の細孔を有する口金より大気中に
押出して自由発泡せしめ発泡体細条を得る。この発泡体
細条を大気中で冷却し引取ロールを通したあと所定角度
を持つように押出方向に対して斜めに切断L、切断した
発泡体細条を発泡炉に導き高温スチームなどで加熱し再
発泡することにより三次元的に湾曲した本発明の熱可塑
性樹脂発泡体のバラ状緩衝体を製造する。(Function) In the bulk cushioning body of the thermoplastic resin foam of the present invention and its manufacture, a screw type extruder is usually used to mix these components and extrude and foam them. That is, a thermoplastic resin, a cell regulator, etc. are fed into an extruder L, heated to a temperature higher than the softening temperature of the thermoplastic resin, kneaded by a screw rotating once, and melted and plasticized. A low-boiling point blowing agent is forced into the vent hole of the extruder using a pump, and the blowing agent is uniformly dispersed in the molten thermoplastic resin by kneading, and then the molten thermoplastic resin composition is cooled to a predetermined temperature. Thereafter, the foam is extruded into the atmosphere through a die having a large number of pores attached to the tip of the extruder to cause free foaming, thereby obtaining foam strips. The foam strips are cooled in the atmosphere, passed through a take-up roll, and then cut at a predetermined angle with respect to the extrusion direction L. The cut foam strips are led to a foaming furnace and heated with high-temperature steam. By re-foaming, a three-dimensionally curved bulk cushioning body of the thermoplastic resin foam of the present invention is manufactured.
(実施例)
以下本発明を実施例にもとづき図を参照しつつ詳細に説
明する。(Example) The present invention will be described in detail below based on an example with reference to the drawings.
MFR=5のポリスチレン100重量部とタルク1.0
重量部を混合したのち、混合物を10kg/時間の割合
で口径50 mmφ、バレル長さ2. 100關の押出
機に供給L、230℃で混線溶融L、押出機のベント孔
よりフロン−11/フロン−22=’50150の組成
の発泡剤をポリスチレンに対して15重量部の割合で高
圧ポンプにより溶融樹脂中に圧入L、更に溶融混合物を
混練し発泡剤を溶融樹脂中に均一に分散させたのち、溶
融組成物を外部より冷却し押出機の先端で150℃とな
L、第7図で示すr = l aysの半円径の押出孔
を22個配列した口金より大気中に押出し自由発泡せし
め、第4図すに示す厚さt = 8 +u、幅W=10
龍の縦断面を持つ連続半円柱状発泡体細条を得た。100 parts by weight of polystyrene with MFR=5 and talc 1.0
After mixing the weight parts, the mixture was poured into a tube having a diameter of 50 mmφ and a barrel length of 2.5 mm at a rate of 10 kg/hour. A blowing agent having a composition of Freon-11/Freon-22 = '50150 is supplied to a 100-degree extruder L, cross-wire melted at 230°C, and a high-pressure pump is added to the polystyrene at a ratio of 15 parts by weight to polystyrene. After the molten mixture is press-fitted into the molten resin, the molten mixture is further kneaded and the blowing agent is uniformly dispersed in the molten resin, the molten composition is cooled from the outside to 150°C at the tip of the extruder, Figure 7. It was extruded into the atmosphere through a nozzle having 22 extrusion holes with a semicircular diameter of r = l ays, and was allowed to freely foam, with a thickness of t = 8 + u and a width of W = 10 as shown in Figure 4.
A continuous semi-cylindrical foam strip with a dragon longitudinal section was obtained.
この発泡体細条を大気中で冷却しつつ引取ロールを通し
たあと、第4図aに示す! = 50 am、 !+=
1/2L、θ1−θ2=20度の形状に斜めに切断L、
ついでこの切断発泡体細条を発泡炉に導き115℃のス
チームで20秒間加熱して再発泡L、第1図a、bに示
すごとく両先端が三次元的に湾曲した形状の本発明のバ
ラ状緩衝体を得た。比較例として発泡体細条を、押出方
向に垂直に第10図c、dに示すごとく小半円柱状に切
断した切断発泡体細条を実施例と同様に操作して第1O
図a、bに示す湾曲のない形状の比較例のバラ状緩衝体
を得た。このようにして得た実施例、比較例のバラ状緩
衝体の特性値を第1表に示す。After passing the foam strip through a take-off roll while cooling in the atmosphere, it is shown in Figure 4a! = 50 am, ! +=
1/2L, cut diagonally into the shape of θ1-θ2 = 20 degrees L,
Next, the cut foam strips were introduced into a foaming furnace and heated with steam at 115° C. for 20 seconds to form a re-foamed L, a rose of the present invention having a three-dimensionally curved shape at both ends as shown in FIG. 1a and b. A shaped buffer was obtained. As a comparative example, cut foam strips were cut into small semi-cylindrical shapes perpendicular to the extrusion direction as shown in FIGS.
A comparative loose shock absorber having a non-curved shape as shown in Figures a and b was obtained. Table 1 shows the characteristic values of the bulk buffer bodies of Examples and Comparative Examples thus obtained.
第8図に示す2 r = 1 mmの円形の押出細孔を
11個配列した口金を使用L、発泡剤としてブタンをポ
リスチレン100重量部に対して8重量部使用した他は
、実施例、比較例−1と同様に操作して得たt2=lO
m諺の連続円柱状発泡体細条を、第5図aに示すt=1
0會m、 E=501II1. Ll−15朋、θ=3
0度に切断して得た実施例の切断発泡体細条、及び押出
発泡体細条を押出方向に垂直にt = 50 amの小
円柱状に切断して得た第11図C1dに示す切断発泡体
細条を、実施例、比較例−1と同様に加熱操作すること
により、第2図に示すごとく両先端が三次元的に湾曲し
た形状の本発明のバラ状j[体、及び第11図C1dに
示すごとく湾曲のない形状の比較例のバラ状v1衝体を
得た。Examples and comparisons were used, except that a die with 11 circular extrusion pores of 2r = 1 mm arranged as shown in Fig. 8 was used, and 8 parts by weight of butane was used as a blowing agent per 100 parts by weight of polystyrene. t2=lO obtained by operating in the same manner as Example-1
The continuous cylindrical foam strip of the proverb is shown in Figure 5a at t = 1.
0 meetings, E=501II1. Ll-15, θ=3
The cut foam strip of the example obtained by cutting at 0 degrees and the cut shown in FIG. 11 C1d obtained by cutting the extruded foam strip into small cylinders at t = 50 am perpendicular to the extrusion direction By heating the foam strips in the same manner as in Examples and Comparative Example-1, the foam strips were heated in the same manner as in Examples and Comparative Example-1 to form loose j [body and no. As shown in FIG. 11 C1d, a loose v1 impactor of a comparative example having a shape without curvature was obtained.
このようにして得たバラ状緩衝体の特性値を第1表に示
す。Table 1 shows the characteristic values of the bulk buffer material thus obtained.
第9図に示すd=1關、四隅は曲率半径=2關の円弧で
ある四角形様の押出細孔を11個配列した口金を使用し
た池は、実施例、比較例−2と同様にして得た第6図に
示す厚さ、幅ともにt=10關の縦断面の連続発泡体細
条を第6図、第12図す、 cのごとく、 θ、=θ
2=22度、 θ嘗=θ2=11度、長さ!=50■l
を持つように、それぞれ斜めに切断したのち実施例、比
較例−2と同様に加熱操作することにより、第3図に示
すごとく両先端が三次元的に湾曲した形状の本発明のバ
ラ状111体、及び第12図a、bに示すごとく湾曲が
少なく本発明の特性値を満たし得ない形状の比較例のバ
ラ状緩衝体を得た。A pond using a die in which 11 rectangular extrusion pores are arranged, where d = 1 angle and the four corners are circular arcs with a radius of curvature = 2, as shown in Fig. 9, was made in the same manner as in Example and Comparative Example-2. The obtained open foam strips of vertical cross section with thickness and width of t = 10 are shown in Fig. 6 and Fig. 12, as shown in c, θ, = θ.
2=22 degrees, θ嘗=θ2=11 degrees, length! =50■l
After cutting each diagonally so as to have a shape of 100 mm, and then heating it in the same manner as in Example and Comparative Example-2, a rose-like shape 111 of the present invention having a three-dimensionally curved shape at both ends as shown in FIG. 3 is obtained. As shown in FIGS. 12a and 12b, comparative loose shock absorbing bodies were obtained which had a shape that did not satisfy the characteristic values of the present invention due to little curvature.
このようにして得たバラ状Ml衝体の特性値を第1表に
示す。Table 1 shows the characteristic values of the loose Ml bombs thus obtained.
第1表に示すように本発明の限定された範囲内の特性値
を示すバラ状緩衝体は、 160mE/g以上の大きな
充填密度を持つものであるが、特性値の限定された範囲
内からはずれた比較例の発泡体の充填密度は90 m
l / g以下と、実施例のバラ状1衝体の充填密度の
1/2以下の数値であることがわかる。As shown in Table 1, the bulk buffer exhibiting characteristic values within the limited range of the present invention has a large packing density of 160 mE/g or more, but the characteristic values within the limited range of The packing density of the foam of the comparative example that was removed was 90 m
It can be seen that the packing density is less than 1/g, which is less than 1/2 of the packing density of the bulk monolayer of the example.
第 1 表
Ocmの段ボール箱に満杯になるようにバラ状緩衝体を
入れ、この満杯量の緩
衝体重量(g>を測定L、段ボール箱
の内容flI(Vmりと(g)との比■m Z / g
を一充填密度とする。Table 1 Put the loose buffer into the cardboard box Ocm until it is full, measure the buffer weight (g) of this full amount, and calculate the ratio of the contents of the cardboard box flI (Vm to (g)). m Z / g
Let be one packing density.
(効果)
本発明は上述のように、両先端が三次元的に湾曲した形
状のバラ状緩衝体であり、三次元的湾曲の少ない形状の
比較例に示した従来技術のバラ状H8体に較べて、収納
容器への充填量が1/2以下で同じ緩衝効果を有する。(Effects) As described above, the present invention is a loose shock absorber having a three-dimensionally curved shape at both ends, and is different from the conventional loose H8 body shown in the comparative example having a shape with less three-dimensional curvature. In comparison, the same buffering effect can be achieved even if the amount filled into the storage container is less than 1/2.
湾曲した紐状の従来技術バラ状緩衝体は、大きく絡み合
った紐状緩衝体同志を手間をかけて小分けしたり、小分
けするため引張って紐が破断し短くなり充填効果が低下
したのに対L、本発明バラ状緩衝体は相互の絡み合いが
ないため、小分けする必要もなく充填効果が低下するお
それもなく、取り扱いやすい。The conventional loose cushioning material in the shape of a curved string requires time and effort to divide the large intertwined string-like cushioning materials into smaller pieces, or when the strings are pulled to be separated into smaller pieces, the strings break and become shorter, reducing the filling effect. Since the bulk cushioning material of the present invention does not become entangled with each other, there is no need to divide it into smaller portions, and there is no fear that the filling effect will deteriorate, making it easy to handle.
本発明バラ状緩衝体の製造方法は、押出機から押出して
発泡せしめて得られた発泡体を、所定範囲の寸法割合及
び所定範囲の角度で斜めに切断L、加熱して再発泡する
。湾曲した紐状の従来技術バラ状[r体製造における急
冷工程を設けるわずられしさもなく、三次元的湾曲の少
ない従来技術バラ状M衝木製造方法と2 はぼ同じ工程
で容易に製造する製造方法であり、産業界に果たす役割
の大きいすぐれた発明である。In the method for manufacturing a bulk cushioning body of the present invention, a foam obtained by extruding and foaming from an extruder is diagonally cut L at a predetermined size ratio and at a predetermined angle, and is re-foamed by heating. Curved string-shaped prior art loose shape [No need for the hassle of quenching step in R-body production, less three-dimensional curvature, prior art loose M cross-shaped manufacturing method and 2 Easily produced in almost the same process This is an excellent invention that will play a large role in industry.
第1〜9図は本発明の詳細な説明する図で、第1〜3図
は実施例1〜3に対応する本発明バラ状緩衝体の斜視図
、第1図すは第1図aを背面よりみた図、第4〜6図a
は再発泡して第1〜3図に示すバラ状緩衝体を形成する
ための、押出発泡体細条を斜めに切断した正面図、第4
〜6図すは第4〜6図aのA−A矢視断面図、第7〜9
図は第4〜6図に示す押出発泡体細条を得るために用い
た口金の押出孔の正面図、第10〜12図は第7〜9図
の口金孔を用いた比較例で、第10図C1第11図C1
第12図すは第7〜9図の口金孔より押出された発泡体
細条を垂直に切断した小片の正面図、第10図d、第1
1図d、第12図Cは第10[Nc、第11図C1第1
2図すのA−A矢視断面図、第10図a、第11図a、
第12図aは第10図C5第11図C1第12図すに示
す小片に切断した発泡体細条を加熱再発泡した発泡体の
斜視図、第10図b、第11図すは第10図a、第11
図aのA−A矢視断面図を示す。
Yは全体幅、しはバラ状緩衝体の長さ、T+は中央部の
肉厚、T2は湾曲した両先端部の肉厚、Wは成形体の幅
、θ5、θ2は切断角、 tは切断体の長さ、1.1は
斜め切断部の水平方向長さ、tは最大厚さ、Wは最大厚
さ部分の幅、rは半円の径、dは四角様の形状の幅、r
Iは四角様の円弧の曲率半径を示す。Figures 1 to 9 are diagrams explaining the present invention in detail, Figures 1 to 3 are perspective views of the bulk cushioning bodies of the present invention corresponding to Examples 1 to 3, Figure 1 is a diagram illustrating Figure 1a. View from the back, Figures 4-6a
4 is a front view of an extruded foam strip cut diagonally for re-foaming to form the bulk cushion shown in FIGS. 1-3; FIG.
Figures 6 to 6 are cross-sectional views taken along the line A-A in Figures 4 to 6a, and Figures 7 to 9.
The figures are front views of the extrusion holes of the die used to obtain the extruded foam strips shown in Figures 4 to 6, and Figures 10 to 12 are comparative examples using the die holes of Figures 7 to 9. Figure 10 C1 Figure 11 C1
Figure 12 is a front view of a small piece cut vertically from the foam strip extruded from the die holes in Figures 7 to 9;
Figure 1 d, Figure 12 C is the 10th [Nc, Figure 11 C1 1st
2. Cross-sectional view taken along line A-A in Figure 2, Figure 10a, Figure 11a,
Figure 12a is a perspective view of a foam obtained by heating and re-foaming the foam strips cut into small pieces as shown in Figure 10C5 Figure 11C1 Figure 12B; Figure a, 11th
A sectional view taken along the line A-A in Figure a is shown. Y is the overall width, the length of the loose buffer, T+ is the thickness at the center, T2 is the thickness at both curved ends, W is the width of the molded body, θ5, θ2 are the cutting angles, and t is The length of the cut body, 1.1 is the horizontal length of the diagonal cut, t is the maximum thickness, W is the width of the maximum thickness, r is the diameter of the semicircle, d is the width of the square shape, r
I indicates the radius of curvature of the quadrangular arc.
Claims (3)
様の曲部の肉厚が両先端から逐次厚くなり中央部で最大
の厚さを示す湾曲した形状で、S字様の長さL、中央部
の肉厚T_1、先端部の肉厚T_2、成形体幅W、全体
幅Yの寸法の割合がT_1/L=0.1〜0.6、T_
1/T_2>2、W/L=0.2〜0.5、Y/L=0
.4〜1.5、Y/W=1.2〜5.0であり、かつ密
度が0.005〜0.05g/mlであることを特徴と
する熱可塑性樹脂発泡体。(1) A thermoplastic resin foam that forms an S-shape. The ratio of length L, center wall thickness T_1, tip wall thickness T_2, molded body width W, and overall width Y is T_1/L=0.1 to 0.6, T_
1/T_2>2, W/L=0.2~0.5, Y/L=0
.. 4 to 1.5, Y/W=1.2 to 5.0, and a density of 0.005 to 0.05 g/ml.
とする請求項1記載の熱可塑性樹脂発泡体。(2) The thermoplastic resin foam according to claim 1, wherein the actual dimension of L is 30 to 100 mm.
より発泡剤を含有する溶融熱可塑性樹脂を大気中に押出
し発泡せしめて得られた発泡体細条を、冷却後押出方向
に斜めに切断し、ついで切断した発泡体細条を加熱し再
発泡することを特徴とする請求項1記載の熱可塑性樹脂
発泡体の製造方法。(3) The molten thermoplastic resin containing a foaming agent is extruded into the atmosphere through a die with multiple pores attached to the tip of the extruder, and the resulting foam strips are cooled and diagonally in the extrusion direction. 2. The method for producing a thermoplastic resin foam according to claim 1, further comprising cutting the foam into strips, and then heating and re-foaming the cut foam strips.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1141493A JPH037318A (en) | 1989-06-03 | 1989-06-03 | Foamable thermoplastic resin and manufacture thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1141493A JPH037318A (en) | 1989-06-03 | 1989-06-03 | Foamable thermoplastic resin and manufacture thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH037318A true JPH037318A (en) | 1991-01-14 |
Family
ID=15293210
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1141493A Pending JPH037318A (en) | 1989-06-03 | 1989-06-03 | Foamable thermoplastic resin and manufacture thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH037318A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5440880A (en) * | 1994-05-16 | 1995-08-15 | Navistar International Transportation Corp. | Diesel engine EGR system with exhaust gas conditioning |
| US5607010A (en) * | 1994-04-26 | 1997-03-04 | MTU Motoren- Und Turbinen-Union Friedrichshafen GmbH | Process for cooling diesel engine exhaust gases |
-
1989
- 1989-06-03 JP JP1141493A patent/JPH037318A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5607010A (en) * | 1994-04-26 | 1997-03-04 | MTU Motoren- Und Turbinen-Union Friedrichshafen GmbH | Process for cooling diesel engine exhaust gases |
| US5440880A (en) * | 1994-05-16 | 1995-08-15 | Navistar International Transportation Corp. | Diesel engine EGR system with exhaust gas conditioning |
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