JPH0148855B2 - - Google Patents
Info
- Publication number
- JPH0148855B2 JPH0148855B2 JP58201760A JP20176083A JPH0148855B2 JP H0148855 B2 JPH0148855 B2 JP H0148855B2 JP 58201760 A JP58201760 A JP 58201760A JP 20176083 A JP20176083 A JP 20176083A JP H0148855 B2 JPH0148855 B2 JP H0148855B2
- Authority
- JP
- Japan
- Prior art keywords
- foam
- cross
- foaming
- cylindrical
- extruder
- 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
Links
- 239000006260 foam Substances 0.000 claims description 22
- 238000005187 foaming Methods 0.000 claims description 10
- 229920005992 thermoplastic resin Polymers 0.000 claims description 9
- 230000001788 irregular Effects 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 238000000465 moulding Methods 0.000 claims description 7
- 238000001125 extrusion Methods 0.000 claims description 6
- 239000011342 resin composition Substances 0.000 claims description 4
- 238000001816 cooling Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 239000005022 packaging material Substances 0.000 description 3
- 229920005672 polyolefin resin Polymers 0.000 description 3
- 238000004513 sizing Methods 0.000 description 3
- 239000004604 Blowing Agent Substances 0.000 description 2
- -1 ethylene glycol Chemical compound 0.000 description 2
- 238000010791 quenching Methods 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- 239000004338 Dichlorodifluoromethane Substances 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000009449 lightweight packaging Methods 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/20—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of indefinite length
- B29C44/22—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of indefinite length consisting of at least two parts of chemically or physically different materials, e.g. having different densities
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/50—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/50—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
- B29C44/507—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying extruding the compound through an annular die
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2023/00—Tubular articles
Landscapes
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
本発明は、軽量包装材、緩衝包装材や断熱材と
して有用な熱可塑性樹脂からなる断面異型の筒状
発泡体を製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a cylindrical foam body of irregular cross-section made of a thermoplastic resin and useful as a lightweight packaging material, a cushioning packaging material, or a heat insulating material.
従来より、物品の保護、緩衝あるいは保温用包
装材として、例えばポリオレフイン系樹脂等の熱
可塑性樹脂を円筒状に発泡させたものが多く用い
られている。 BACKGROUND ART Conventionally, cylindrical foamed thermoplastic resins such as polyolefin resins have often been used as packaging materials for protection, cushioning, or heat retention of articles.
このような円筒状発泡体を連続的に製造する方
法としては発泡性熱可塑性樹脂組成物を押出成形
する方法が広く行われている。用途の拡大につ
れ、断面異型を有する発泡体が必要とされる場合
も多くなり、そのような異型断面を有する筒状あ
るいは棒状発泡体を製造するためには、従来から
発泡性熱可塑性樹脂組成物を特殊な形状の成形口
金を通して押出成形しつつ発泡させる方法、ある
いは通常の押出機により断面真円状に押出成形
し、これをサイジング装置を通して異型断面に賦
形する方法が行われていた。 As a method for continuously producing such a cylindrical foam, a method of extrusion molding a foamable thermoplastic resin composition is widely used. As applications expand, foams with irregular cross-sections are often required, and in order to manufacture cylindrical or rod-shaped foams with such irregular cross-sections, foamable thermoplastic resin compositions have traditionally been used. The conventional method is to extrude and foam the material through a specially shaped molding die, or to extrude it into a perfect circular cross section using a normal extruder, and then shape it into an irregular cross section through a sizing device.
しかしながら、前者の方法においては、特に長
尺のものを製造する、断面形状が一定したものを
得ることが難しく、長さ方向に断面形状のばらつ
きが多くなり易いという問題があつた。 However, in the former method, there is a problem that it is difficult to manufacture a long product with a uniform cross-sectional shape, and the cross-sectional shape tends to vary widely in the length direction.
また、長尺のものでなくとも発泡倍率が15〜40
倍程度の高倍率発泡体においては、熱可塑性樹脂
の流れや発泡方向を口金の断面形状の変化により
調節することが非常に困難なため、この方法を用
いて実用化されているのは、円形あるいは円筒形
断面を持つた発泡体のみである。後者のサイジン
グ装置を用いる方法では、大型で複雑な装置を必
要とするという問題があつた。 In addition, even if it is not a long one, the foaming ratio is 15 to 40.
In the case of foams with a high magnification of about 2.5 times, it is extremely difficult to control the flow and foaming direction of the thermoplastic resin by changing the cross-sectional shape of the die. Or just a foam with a cylindrical cross section. The latter method using a sizing device has the problem of requiring a large and complicated device.
特に、高倍率発泡体製造の場合には、サイジン
グ装置内面での滑り性の確保のために潤滑剤を流
したり、加圧空気層を作る等の多大な工夫を要
し、従つて、さらに大型で複雑な装置が必要とな
つてしまう。 In particular, in the case of manufacturing high-magnification foams, great efforts are required such as pouring lubricant and creating a pressurized air layer to ensure slipperiness on the inside of the sizing device, which results in even larger products. This requires complicated equipment.
本発明はこれらの問題を解決するためになされ
たもので、上記のような複雑な設備や難度の高い
技術を必要とせずに、断面異型の高倍率発泡体を
連続的に製造する方法を提供することを目的とす
る。 The present invention was made to solve these problems, and provides a method for continuously manufacturing high-magnification foams with irregular cross-sections without requiring the above-mentioned complicated equipment or highly difficult techniques. The purpose is to
すなわち本発明の断面異型の発泡体の製造方法
は、所定量の発泡剤を含有する熱可塑性樹脂組成
物を押出機により筒状あるいは棒状に連続的に押
出成形しつつ発泡させるに当たり、押出機の成形
口金近傍において押出成形直後の成形体を局部的
に急冷し、発泡を抑制することを特徴とする。 That is, the method for producing a foam with an irregular cross-section of the present invention involves continuously extruding and foaming a thermoplastic resin composition containing a predetermined amount of a blowing agent into a cylindrical or rod shape using an extruder. It is characterized by locally rapidly cooling the molded product immediately after extrusion molding in the vicinity of the molding die to suppress foaming.
以下本発明の詳細をその一実施例を示す図面を
参照つつ説明する。 The details of the present invention will be explained below with reference to the drawings showing one embodiment thereof.
第1図に示すように、符号1は押出機で、この
押出機1の円筒形断面を有する成形口金2の吐出
孔3に隣接し、樹脂の押出される方向と直角の方
向に開口する冷却管4が取付けられている。押出
機1より円筒状に押出成形された熱可塑性樹脂5
は吐出さされた直後に発泡を開始するが、冷却管
4から吐出される冷却媒体により急冷される部分
6のみは発泡を抑制され、その結果、第2図に示
されたような断面を有する連続した発泡体が得ら
れる。 As shown in FIG. 1, reference numeral 1 denotes an extruder, which is adjacent to the discharge hole 3 of the molding die 2 having a cylindrical cross section, and has a cooling hole that opens in a direction perpendicular to the direction in which the resin is extruded. A tube 4 is attached. Thermoplastic resin 5 extruded into a cylindrical shape by an extruder 1
starts foaming immediately after being discharged, but only the portion 6 that is rapidly cooled by the cooling medium discharged from the cooling pipe 4 is suppressed from foaming, and as a result, has a cross section as shown in FIG. A continuous foam is obtained.
吐出された成形体を局部的に急冷する方法とし
ては、急冷の度合急冷する表面の広さに応じ圧縮
空気を吹付する方法、水塗りの工法あるいはエチ
レングリコール等のアルコールを用いる方法等、
発泡を抑制する効果のある急冷方法であれば、特
に限定されない。さらに冷却個所または冷却面積
を増せば種々の断面形状の発泡体を製造すること
が可能である。 Methods for locally quenching the discharged molded product include spraying compressed air depending on the degree of quenching and the area of the surface to be quenched, a water coating method, a method using alcohol such as ethylene glycol, etc.
Any rapid cooling method is not particularly limited as long as it is effective in suppressing foaming. Furthermore, by increasing the number of cooling points or cooling areas, it is possible to produce foams with various cross-sectional shapes.
実施例 1
MFR5の低密度ポリエチレンに、発泡剤として
ジクロロジフルオロメタンを30重量部配合してな
る組成物を、第1図に示すごとき外径50mmの押出
機に供給し、円筒状の外型の中央にほぼ円柱状の
内型が固定ブリツジにより隔離配置された構造の
成形口金2を通して、前記発泡剤入りポリエチレ
ン組成物を、この成形金型内から真円形状の成形
口金2を通し、15.0Kg/Hrの速度で押出成形し
つつ約30倍に発泡させ、同時に口金の前方上面よ
り、冷却管4から冷却水を噴出させた。Example 1 A composition consisting of MFR5 low-density polyethylene mixed with 30 parts by weight of dichlorodifluoromethane as a blowing agent was supplied to an extruder with an outer diameter of 50 mm as shown in Fig. 1, and a cylindrical outer mold was formed. The foaming agent-containing polyethylene composition was passed through the molding die 2, which had a structure in which a substantially cylindrical inner mold was separated by a fixed bridge in the center, and was passed through the perfectly circular forming die 2 from within the molding die, to a total weight of 15.0 kg. The foam was expanded approximately 30 times while extrusion molding was carried out at a speed of /Hr, and at the same time, cooling water was jetted from the cooling pipe 4 from the front upper surface of the die.
こうして第2図に示すような、上面が発泡が抑
止され、内部空隙部もほぼ同一形状とした半円状
のポリオレフイン系樹脂発泡筒体が得られた。 In this way, a semicircular polyolefin-based resin foam cylinder was obtained, as shown in FIG. 2, in which foaming was suppressed on the upper surface and the internal voids were also of substantially the same shape.
実施例 2
実施例1と同じ組成物を同一条件で押出成形
し、押出口金の前方で3方向より、圧縮空気を噴
出させ、約30倍の倍率に発泡させて、第3図に示
す三角形の筒状体を得られた。Example 2 The same composition as in Example 1 was extruded under the same conditions, and compressed air was blown out from three directions in front of the extrusion die to foam at a magnification of about 30 times, forming the triangle shown in Figure 3. A cylindrical body was obtained.
実施例 3
実施例1と同じ組成物を同一条件で押出成形
し、押出口金の前方で4方向より、圧縮空気を噴
出させ、第4図に示す断面四角形状ポリオレフイ
ン系樹脂発泡筒体が得られた。Example 3 The same composition as in Example 1 was extruded under the same conditions, and compressed air was blown out from four directions in front of the extrusion die to obtain a polyolefin resin foam cylinder having a square cross section as shown in FIG. It was done.
以上の実施例からも明らかなように本発明によ
れば、複雑な装置や高度な操作技術を必要とせず
に、様々な異型断面の発泡体を安定してかつ連続
的に製造することができる。 As is clear from the above examples, according to the present invention, foams with various irregular cross sections can be stably and continuously produced without the need for complicated equipment or advanced operating techniques. .
第1図は本発明の製造を説明するための斜視
図、第2図は第1図の押出機により製造された発
泡体の断面図、第3図は3個所冷却により得られ
る発泡体の断面図、第4図は4個所冷却により得
られる発泡体の断面図である。
1……押出機、2……成形口金、3……吐出
孔、4……冷却管、5……熱可塑性樹脂、6……
急冷される部分。
Fig. 1 is a perspective view for explaining the production of the present invention, Fig. 2 is a cross-sectional view of the foam produced by the extruder shown in Fig. 1, and Fig. 3 is a cross-section of the foam obtained by cooling at three locations. FIG. 4 is a sectional view of a foam obtained by cooling at four locations. 1... Extruder, 2... Molding die, 3... Discharge hole, 4... Cooling pipe, 5... Thermoplastic resin, 6...
The part that is rapidly cooled.
Claims (1)
状あるいは棒状に連続的に押出成形しつつ発泡さ
せるに当たり、押出機の成形口金近傍において押
出成形直後の成形体を局部的に急冷し、発泡を抑
制することを特徴とする断面異型の発泡体の製造
方法。1. When foaming a foamable thermoplastic resin composition while continuously extruding it into a cylindrical or rod shape using an extruder, the molded product immediately after extrusion is locally quenched near the molding die of the extruder to prevent foaming. A method for producing a foam with an irregular cross-section, characterized by suppressing the shape of the foam.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58201760A JPS6092825A (en) | 1983-10-26 | 1983-10-26 | Manufacture of foam with odd-shaped section |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58201760A JPS6092825A (en) | 1983-10-26 | 1983-10-26 | Manufacture of foam with odd-shaped section |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6092825A JPS6092825A (en) | 1985-05-24 |
JPH0148855B2 true JPH0148855B2 (en) | 1989-10-20 |
Family
ID=16446479
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58201760A Granted JPS6092825A (en) | 1983-10-26 | 1983-10-26 | Manufacture of foam with odd-shaped section |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6092825A (en) |
-
1983
- 1983-10-26 JP JP58201760A patent/JPS6092825A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6092825A (en) | 1985-05-24 |
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