JPS638892B2 - - Google Patents

Info

Publication number
JPS638892B2
JPS638892B2 JP58026224A JP2622483A JPS638892B2 JP S638892 B2 JPS638892 B2 JP S638892B2 JP 58026224 A JP58026224 A JP 58026224A JP 2622483 A JP2622483 A JP 2622483A JP S638892 B2 JPS638892 B2 JP S638892B2
Authority
JP
Japan
Prior art keywords
foaming
foam
molded body
foamed
high frequency
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
Application number
JP58026224A
Other languages
Japanese (ja)
Other versions
JPS59152827A (en
Inventor
Tooru Nishihata
Yoshuki Nishi
Kazuhiko Fujiwara
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.)
Sumitomo Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite 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 Sumitomo Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP58026224A priority Critical patent/JPS59152827A/en
Publication of JPS59152827A publication Critical patent/JPS59152827A/en
Publication of JPS638892B2 publication Critical patent/JPS638892B2/ja
Granted 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
    • B29C44/56After-treatment of articles, e.g. for altering the shape
    • 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
    • B29C44/36Feeding the material to be shaped
    • B29C44/46Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
    • B29C44/50Feeding 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
    • B29C44/505Feeding 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 a flat die

Landscapes

  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】 本発明は連続的に発泡体を製造する方法に関す
るものであり、更に詳細には、熱可塑性樹脂から
なり、加熱により発泡しかつ高周波をかける事で
内部発熱により発泡し得る性質を有する成形体を
素材としてこれを連続的に発泡体にする方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for continuously manufacturing a foam, and more specifically, the present invention relates to a method for continuously manufacturing a foam, and more specifically, a foam is made of a thermoplastic resin and is foamed by heating and foamed by internal heat generation by applying high frequency. The present invention relates to a method of continuously forming a foamed body from a molded body having the properties that can be obtained.

又、以上の性質を有する成形体であれば成形体
の形状は板状、ロツド、異形、チユーブなどどの
ような形状のものでも連続的に発泡体を製造でき
る事を特徴とするものである。
Further, the molded product having the above-mentioned properties is characterized in that a foamed product can be continuously produced regardless of the shape of the molded product, such as plate, rod, irregular shape, or tube.

ポリエチレン等の熱可塑性樹脂からなり、加熱
により発泡し得る性質、すなわち発泡能力を有す
る成形体を加熱発泡させて板状発泡体を製造する
方法として、従来種々の提案がなされている。
Various proposals have been made in the past as a method for producing a plate-shaped foam by heating and foaming a molded body made of a thermoplastic resin such as polyethylene and having the property of being foamable by heating, that is, the ability to foam.

例えば、成形体を垂直に降下させながら加熱し
て発泡を行うといういわゆる縦型発泡法とか或い
は、成形体を先ず支持用ベルト上で加熱し、次い
で自由な状態で発泡を完成させるといういわゆる
横型発泡法が知られている。上述のような方法
は、発泡能を有する成形体を空気中で発泡させ得
るという点で液体の熱媒中で発泡させる方法に比
して利点を有している。
For example, there is the so-called vertical foaming method, in which the molded product is heated and foamed while falling vertically, or the so-called horizontal foaming method, in which the molded product is first heated on a support belt and then foamed in a free state. The law is known. The method described above has an advantage over the method of foaming in a liquid heat medium in that a foamable molded article can be foamed in air.

しかし横型発泡法は支持ベルト上で加熱された
成形体が発泡開始の直前、又は直後に該支持ベル
トから離された段階での支持が困難である。その
段階ではすでに発泡が始まつており、当然元の成
形体よりも幅、長さ及び厚さが増大し、未発泡状
態から発泡状態へ移る過渡的な段階では成形体は
波打ち状態を呈し凹凸を生じる。このような状態
の成形体或いは発泡体を支持するのは噴出気流等
の手段によつても困難であり、安定した支持或い
は移動を行い難い。又、この方法を実施する場合
装置全体の長さが大きくなり大規模な装置を用意
する必要があつて敷地等に制約があれば実用的で
ない。
However, in the horizontal foaming method, it is difficult to support the molded article heated on the support belt at the stage when it is separated from the support belt immediately before or immediately after the start of foaming. At that stage, foaming has already begun, and naturally the width, length, and thickness of the molded product increase compared to the original molded product, and in the transitional stage from an unfoamed state to a foamed state, the molded product exhibits a wavy state and becomes uneven. occurs. It is difficult to support a molded body or foamed body in such a state even by means such as jet air, and it is difficult to stably support or move the body. Furthermore, when implementing this method, the length of the entire device increases, it is necessary to prepare a large-scale device, and it is not practical if there are restrictions on the site or the like.

又、縦型発泡法においては未発泡の成形体を垂
直に吊した状態で加熱発泡させるが、内部まで発
泡させるためには加熱温度を高くするか長い加熱
距離が必要である。そのため、軟化した成形体は
自重により伸び、従つて発泡後の気泡は成形体の
長さ方向に延伸された状態となる。このような発
泡体は後の加工において加熱すると収縮するた
め、製品の寸法安定性が悪いという欠点を有す
る。また、上記を併用した発泡法も考えられてい
る。つまり、成形体を水平に支持した状態で予熱
した後、該予熱温度よりも高温域中を垂直方向に
降下もしくは上昇させながら発泡せしめ、次いで
再び水平に支持しながら加熱して発泡を完了させ
る発泡法である。
In the vertical foaming method, an unfoamed molded product is suspended vertically and heated to foam, but in order to foam the inside, a high heating temperature or a long heating distance is required. Therefore, the softened molded body stretches under its own weight, and therefore, the bubbles after foaming are in a state of being stretched in the length direction of the molded body. Such foams shrink when heated during subsequent processing, resulting in poor dimensional stability of the product. A foaming method that uses the above methods in combination is also being considered. In other words, the molded body is preheated while being supported horizontally, then foamed while falling or rising vertically in a higher temperature range than the preheating temperature, and then heated again while being supported horizontally to complete foaming. It is the law.

この方法も、水平に支持した状態で予熱するこ
とにより、多大なエネルギーを消費し、装置の長
さが大きくなり、大規模な装置が必要になる。
又、成形品の厚みが大きくなる程、成形品の内部
への熱伝導が悪くなり、その分だけ、装置の大規
模化を招くという欠点を有する。
This method also consumes a large amount of energy due to preheating in a horizontally supported state, increases the length of the device, and requires a large-scale device.
Furthermore, as the thickness of the molded product increases, heat conduction into the interior of the molded product becomes poorer, resulting in a corresponding increase in the scale of the apparatus.

本発明は、上述したような従来の発泡方法に存
する欠点をカバーするためになされたものであ
り、かつ発泡倍率を自由に最大限20倍程度まで均
一に保持しうる装置を使用する方法を提供するこ
とを目的とする。
The present invention has been made to overcome the drawbacks of the conventional foaming methods as described above, and provides a method using an apparatus that can freely maintain the foaming ratio uniformly up to a maximum of about 20 times. The purpose is to

すなわち本発明は、連続的に供給される発泡能
を有する熱可塑性樹脂成形体を発泡後の成形体の
延伸を防ぐため押出機より押出し得る温度をでき
るだけ低い温度で押出し、ついで押出し温度より
高温域中を該成形体の表面が他の器物に接触する
ことなく垂直方向に降下させながら徐々に発泡さ
せ、そしてそのまま垂直に降下させながら、成形
体内部を高周波で加熱して発泡を完了させること
を特徴とする連続的に発泡体を製造する方法を要
旨とするものである。
That is, in the present invention, a continuously supplied thermoplastic resin molded body having foaming ability is extruded from an extruder at a temperature as low as possible to prevent stretching of the molded body after foaming, and then extruded in a temperature range higher than the extrusion temperature. The inside of the molded body is gradually foamed while being lowered vertically without the surface of the molded body coming into contact with other utensils, and the inside of the molded body is heated with high frequency while the molded body is lowered vertically to complete the foaming. The gist of this paper is a method for continuously producing a foam, which is characterized by its characteristics.

本発明において用いられる熱可塑性樹脂成形体
とは、前述したように加熱することで軟化し、か
つ高周波をかけることで発熱を起し、次いで含有
されている発泡剤の分解に併つて発泡し得る性質
を有する熱可塑性樹脂の成形体を言い、その成形
体の形状は、板状、ロツド、異形、チユーブと称
される形状を含むものである。
As mentioned above, the thermoplastic resin molded article used in the present invention can be softened by heating, generate heat by applying high frequency, and then foam as the foaming agent contained therein decomposes. It refers to a molded body of thermoplastic resin having properties, and the shape of the molded body includes shapes called plate, rod, irregular shape, and tube.

又、上記成形体を製造する手段についても特に
限られず、押出成形等によつて製造されたもので
もよく、連続長尺体になされたものが特に良い。
本発明に使用する熱可塑性樹脂としては、ポリ塩
化ビニル、ゲル分を含有する塩化ビニル樹脂組成
物、エチレン―塩化ビニル共重合体、熱可塑性エ
ラストマーなど高周波により内部発熱が可能なも
のであれば限定されない。
Further, the means for producing the molded body is not particularly limited, and it may be manufactured by extrusion molding or the like, and a continuous elongated body is particularly preferable.
Thermoplastic resins used in the present invention are limited to those that can generate internal heat under high frequency, such as polyvinyl chloride, vinyl chloride resin compositions containing gel components, ethylene-vinyl chloride copolymers, and thermoplastic elastomers. Not done.

以上述べたような発泡能を有する熱可塑性樹脂
成形体は、発泡剤以外に必要に応じて可塑剤、安
定剤、発泡助剤、顔料等が含有されていても良い
ことは言うまでもない。
It goes without saying that the thermoplastic resin molded article having foamability as described above may contain a plasticizer, a stabilizer, a foaming aid, a pigment, etc., as necessary, in addition to the foaming agent.

次に本発明を更に具体的に説明するために本発
明の実施に際しての装置例を示す図面を参照しな
がら詳説する。
Next, in order to explain the present invention more specifically, the present invention will be explained in detail with reference to the drawings showing an example of an apparatus for carrying out the present invention.

第1図は、本発明方法に使用する装置を示す縦
断面図であり、成形体を垂直に降下さる方法を採
るものである。
FIG. 1 is a longitudinal sectional view showing an apparatus used in the method of the present invention, which employs a method in which a molded body is vertically lowered.

同図において発泡装置は、垂直な発泡室1及び
2とから構成されており、1には加熱器3が1
対、2には高周波装置4が1対設けられている。
加熱器には、例えば赤外線ランプとか電熱ヒータ
ーとか或いは熱風噴出装置等が用いられる。
In the figure, the foaming device is composed of vertical foaming chambers 1 and 2, and 1 has a heater 3 installed in it.
A pair of high frequency devices 4 are provided in pair 2.
As the heater, for example, an infrared lamp, an electric heater, a hot air blower, or the like is used.

前述したような発泡能を有する熱可塑性成形体
5は、押出機6より連続的に押出し得る温度好ま
しくはできるだけ低い温度で発泡室1に送り込ま
れる。発泡室1は図示するように垂直に設けら
れ、その発泡室1内の一対の加熱器3の間を成形
体がその表面が他の器物に接触することなく通過
するべくなされており、成形体はそこで徐々に発
泡し発泡体7となる。発泡を起こさせるため、通
常行われているように、成形体に含まれる発泡剤
の分解温度以上で発泡が徐々に行われるような温
度に発泡室を加熱しておく。この時の温度も一義
的に定めることはできず成形体の樹脂の種類とか
発泡剤の種類等によつて異なる。
The thermoplastic molded body 5 having the above-mentioned foamability is fed into the foaming chamber 1 at a temperature that allows continuous extrusion from the extruder 6, preferably at a temperature as low as possible. As shown in the figure, the foaming chamber 1 is provided vertically, and the molded article is configured to pass between a pair of heaters 3 in the foaming chamber 1 without its surface coming into contact with other utensils. There, it gradually foams to form the foam 7. In order to cause foaming, the foaming chamber is heated to a temperature at which foaming is gradually carried out above the decomposition temperature of the foaming agent contained in the molded article, as is usually done. The temperature at this time cannot be unambiguously determined either, but varies depending on the type of resin of the molded article, the type of blowing agent, etc.

発泡室1内で発泡が本格的に始まると、成形体
はその体積を増し、従つて成形体の幅、長さ及び
肉厚が増大するが上述のように成形体5或いは発
泡体7を他の器物に接触させることなく移動する
ことができる。このため、軟化状態にある発泡体
7の表面は、何ら損傷を受けることなく製品化さ
れる。
When foaming begins in earnest in the foaming chamber 1, the volume of the molded body increases, and therefore the width, length, and wall thickness of the molded body increase. can be moved without coming into contact with other objects. Therefore, the surface of the foam 7 in a softened state is manufactured into a product without any damage.

この成形体は、次いで加熱室2に供給され、高
周波装置の極板間4を通ることで、安定した又、
望むなら高倍率の発泡体8となつて製品化され、
支持ロール10及び11を通つて引取りロール9
により引取られ製品として取り出される。
This molded body is then supplied to the heating chamber 2, and is stabilized by passing through the plate gap 4 of the high frequency device.
If desired, it can be made into a product with a high magnification foam 8,
Take-off roll 9 passes through support rolls 10 and 11
It is picked up by the company and taken out as a product.

高周波装置4は、発泡体7の未反応発泡剤―特
に中心部の―を分解させることを目的としてい
る。
The high frequency device 4 is intended to decompose unreacted blowing agent in the foam 7, especially in the center.

発泡室1及び2の長さ、つまり降下距離につい
ては、自重により発泡した気泡の延伸が心配され
るため短かい方が良いと考えるのは当然である。
この方法では、特に発泡室1で徐々に成形体を発
泡させ、未発泡部―特に中心部―は、次の発泡室
2で高周波により発泡させるため、発泡室1の温
度は、従来の縦型発泡の場合の加熱温度より低
く、長さを短かくでき、そして発泡体の中心部が
未発泡のまま降下させる割合が長いため、自重に
よる発泡した気泡の延伸を防ぐことができる。
Regarding the lengths of the foaming chambers 1 and 2, that is, the descending distance, it is natural to think that the shorter the length, the better, since there is a concern that the foamed bubbles may stretch due to their own weight.
In this method, the molded product is gradually foamed especially in the foaming chamber 1, and the unfoamed part (especially the center part) is foamed in the next foaming chamber 2 by high frequency, so the temperature of the foaming chamber 1 is lower than that of the conventional vertical type Since the heating temperature is lower than that for foaming, the length can be shortened, and the center of the foam is allowed to fall unfoamed for a long time, it is possible to prevent the foamed cells from stretching due to their own weight.

これらの発泡室の長さ及び加熱温度は、成形体
の種類及び発泡挙動により適宜定める。又、押出
した樹脂の温度は発泡剤の発泡温度以下であるこ
とは当然であるが、好ましくはできるだけ低くし
ておくことが必要である。
The length and heating temperature of these foaming chambers are appropriately determined depending on the type of molded product and foaming behavior. Although it is natural that the temperature of the extruded resin is below the foaming temperature of the blowing agent, it is preferably kept as low as possible.

本発明は、以上に詳説したように、成形体を押
出機より押出し得る温度で押出し、高温域中を該
成形体の表面が他の器物に接触することなく垂直
方向に降下させながら徐々に発泡させ、次いでそ
のまま降下させながら高周波で加熱して発泡を完
了させるという工程を採用するものである。その
ため以下に述べるような作用効果を持つている。
As explained in detail above, the present invention involves extruding a molded product from an extruder at a temperature that allows extrusion, and gradually foaming the molded product while lowering the molded product vertically in a high temperature range without contacting other utensils. This method employs a process of heating the foam with high frequency while lowering the foam to complete foaming. Therefore, it has the following effects.

押出機より直接発泡室へ送られるため熱効率が
良く、しかも成形体が他の器物に接触することな
く垂直に吊下げた状態で発泡せしめるから、発泡
しようとする成形体は自由に発泡することがで
き、成形体の体積が増大する過程で生じるしわを
外力によつてつぶしたり互いに接触させることが
ない。このため軟化状態にある発泡体の表面に損
傷を与えることがなく、表面状態の良い発泡体を
製造することができる。又、加熱発泡室において
成形体を徐々に発泡させ、特に中心部を未発泡の
状態で吊下げるため、自重による気泡の延伸を防
ぐことができる。そして最終段階で、未反応の発
泡剤を高周波で分解するため、発泡した気泡が均
一で、発泡倍率が高いものまで得ることができ
る。
Thermal efficiency is high because the foam is sent directly from the extruder to the foaming chamber, and since the molded product is foamed while hanging vertically without coming into contact with other objects, the molded product to be foamed can freely foam. This prevents wrinkles that occur during the process of increasing the volume of the molded product from being crushed by external force or causing them to come into contact with each other. Therefore, the surface of the foam in a softened state is not damaged, and a foam with good surface condition can be manufactured. In addition, since the molded body is gradually foamed in the heating and foaming chamber, and the center portion in particular is hung in an unfoamed state, it is possible to prevent the bubbles from stretching due to their own weight. In the final stage, the unreacted foaming agent is decomposed using high frequency waves, making it possible to produce uniform foamed cells with a high expansion ratio.

更に本発明方法を実施する場合に、発泡段階を
垂直方向の移動で行い得るので、少し高さは必要
となるが狭い敷地でも装置を設置することができ
好適である。
Furthermore, when carrying out the method of the present invention, the foaming step can be carried out by moving in the vertical direction, so although a little height is required, the apparatus can be installed even in a narrow site, which is suitable.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明を実施するための装置の一例
を示すもので、図中主たる部分の番号は、以下の
通りである。 1,2は発泡室、3は加熱器、4は高周波装
置、5は成形体、6は押出機、7,8は発泡体、
9は引取りロール、10,11は支持ロール。
FIG. 1 shows an example of an apparatus for carrying out the present invention, and the main parts in the figure are numbered as follows. 1 and 2 are foaming chambers, 3 is a heater, 4 is a high frequency device, 5 is a molded product, 6 is an extruder, 7 and 8 are foams,
9 is a take-up roll, and 10 and 11 are support rolls.

Claims (1)

【特許請求の範囲】 1 押出機より連続的に押出される発泡能力を有
する熱可塑性樹脂成形体を、押出し温度より高温
域中に垂直方向に降下させながら発泡させ、更に
成形体内部を高周波で加熱して発泡を完了させ、
冷却固化して連続的に製品を得ることを特徴とす
る発泡体の製造方法。 2 熱可塑性樹脂が高周波により発熱可能な樹脂
であることを特徴とする特許請求の範囲第1項記
載の発泡体の製造方法。 3 高周波により発熱可能な樹脂が、塩化ビニル
系樹脂組成物であることを特徴とする特許請求の
範囲第2項記載の発泡体の製造方法。
[Claims] 1. A thermoplastic resin molded body having a foaming ability that is continuously extruded from an extruder is foamed while falling vertically into a region higher than the extrusion temperature, and the inside of the molded body is further heated with high frequency. Heat to complete foaming,
A method for producing a foam characterized by continuously obtaining a product by cooling and solidifying. 2. The method for producing a foam according to claim 1, wherein the thermoplastic resin is a resin that can generate heat using high frequency waves. 3. The method for producing a foam according to claim 2, wherein the resin capable of generating heat by high frequency is a vinyl chloride resin composition.
JP58026224A 1983-02-21 1983-02-21 Manufacture of foamed body Granted JPS59152827A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58026224A JPS59152827A (en) 1983-02-21 1983-02-21 Manufacture of foamed body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58026224A JPS59152827A (en) 1983-02-21 1983-02-21 Manufacture of foamed body

Publications (2)

Publication Number Publication Date
JPS59152827A JPS59152827A (en) 1984-08-31
JPS638892B2 true JPS638892B2 (en) 1988-02-25

Family

ID=12187405

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58026224A Granted JPS59152827A (en) 1983-02-21 1983-02-21 Manufacture of foamed body

Country Status (1)

Country Link
JP (1) JPS59152827A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0725123B2 (en) * 1986-08-04 1995-03-22 ダウ化工株式会社 Method for producing styrene resin foam
JPH0431024A (en) * 1990-05-29 1992-02-03 Toray Ind Inc Manufacture of microporous sheet

Also Published As

Publication number Publication date
JPS59152827A (en) 1984-08-31

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