JP2602447B2 - Method for foaming thermoplastic resin - Google Patents

Method for foaming thermoplastic resin

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Publication number
JP2602447B2
JP2602447B2 JP63100124A JP10012488A JP2602447B2 JP 2602447 B2 JP2602447 B2 JP 2602447B2 JP 63100124 A JP63100124 A JP 63100124A JP 10012488 A JP10012488 A JP 10012488A JP 2602447 B2 JP2602447 B2 JP 2602447B2
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JP
Japan
Prior art keywords
steam
mold
valve
thermoplastic resin
pressure
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
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JP63100124A
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Japanese (ja)
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JPH01271225A (en
Inventor
芳彦 関
Original Assignee
芳彦 関
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Priority to JP63100124A priority Critical patent/JP2602447B2/en
Publication of JPH01271225A publication Critical patent/JPH01271225A/en
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Publication of JP2602447B2 publication Critical patent/JP2602447B2/en
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、プラスチック発泡体などの熱可塑性合成樹
脂の発泡体、殊にブロックを成形する際に、加熱蒸気調
節操作により金型内で発泡成形品を製造する発泡成形方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for foaming a thermoplastic synthetic resin such as a plastic foam, particularly a block, in a mold by heating steam control operation in a mold. The present invention relates to a foam molding method for producing a molded article.

〔従来の技術〕[Conventional technology]

発泡成形品の製造は、金型を使用して発泡性の熱可塑
性樹脂粒子(ビーズ)を予備発泡し、又は予備発泡させ
ることなく、金型内に充填して加熱成形した後、冷却し
て離型後に乾燥させることが一般的である。この従来の
発泡成形では、型閉めし、ビーズを金型内に充填してブ
ローバックし、蒸気加熱して発泡成形し、予冷後に水道
水などの低温の冷却水をもって水冷して放冷で自然冷却
後離型するスチームチェスト法が多用されている。
In the production of a foamed molded product, foaming thermoplastic resin particles (beads) are pre-foamed using a mold, or without being pre-foamed, filled in a mold, heated, and then cooled. It is common to dry after release. In this conventional foam molding, the mold is closed, the beads are filled in a mold, blow-backed, foam-formed by steam heating, pre-cooled, then cooled with tap water or other low-temperature cooling water and allowed to cool naturally. A steam chest method of releasing after cooling is often used.

ところが、この方法でつくられる発泡成形方法におい
ては、加熱蒸気室の容積が一定であるため、室内の蒸気
温度は蒸気圧力に正比例するので、蒸気温度を調節する
ため蒸気圧力の調整を行われている。
However, in the foam molding method produced by this method, since the volume of the heated steam chamber is constant, the steam temperature in the chamber is directly proportional to the steam pressure, so that the steam pressure is adjusted to adjust the steam temperature. I have.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

しかしながら、従来の蒸気加熱方法では、比較的高圧
(0.6〜0.8kg/cm2G)で成形されていて、サイクル的に
は発泡成形製品のブロック重量によりは若干異なるが、
20分前後の長時間を要し、生産性を向上させることがで
きなかった。また、調圧機構が一定に保たれるので、常
に一定の蒸気供給しかできず、原料ビーズのガス抜きを
含め加熱成形サイクルタイムが相当かかり、成形一サイ
クル毎に限界があって生産性をあげることができないば
かりか、不便な位置関係で蒸気供給調整の操作がやっか
いであるなど問題であった。
However, in the conventional steam heating method, molding is performed at a relatively high pressure (0.6 to 0.8 kg / cm 2 G), and the cycle varies slightly depending on the block weight of the foam molded product.
It took a long time, about 20 minutes, to improve productivity. In addition, since the pressure regulating mechanism is kept constant, only constant steam supply is possible at all times, and considerable time is required for heat molding cycle time, including degassing of raw material beads, and there is a limit for each molding cycle, increasing productivity. In addition to the inability to perform such operations, the operation of adjusting the steam supply was inconvenient due to the inconvenient positional relationship.

本発明は、これら従来の欠点を排除しようとするもの
で、雄金型、雌金型を個別で部分的にスチーム圧の調圧
が可能で、蒸気供給時間の短縮化とビーズのガス抜きを
容易にし、生産性を大幅に向上させ、成形作業をも容易
迅速にして生産効率を良好にするとともに、調整作業も
ひんぱんに行う必要がなく、自動調整が可能で、設備的
にも煩雑な制約がなく、安価な構成にでき安全で安定し
た発泡成形作業ができる方法を提供することを目的とし
たものである。
The present invention is intended to eliminate these conventional disadvantages, and it is possible to individually and partially adjust the steam pressure of the male mold and the female mold, thereby shortening the steam supply time and degassing the beads. It facilitates, greatly improves productivity, makes molding work easier and quicker, improves production efficiency, and eliminates the need for frequent adjustments, allows automatic adjustments, and requires complicated facilities. It is an object of the present invention to provide a method capable of performing a safe and stable foam molding operation with an inexpensive configuration without any trouble.

〔課題を解決するための手段〕[Means for solving the problem]

本発明においては、上述の目的を達成するため、蒸気
チャンバを備えた雄金型及び雌金型、或いは雌金型同士
を接離可能に対向させて形成するキャビティ内において
発泡性熱可塑性樹脂粒子を加熱して発泡融着させる方法
において、前記雄金型及び雌金型中の少なくともいずれ
か一方の金型にある蒸気チャンバを複数に独立した蒸気
チャンバに区画し、各蒸気チャンバ毎に開閉弁のある蒸
気供給路と、開閉弁のあるドレーン排出路と、さらに開
閉弁のある真空ポンプに連なる吸引流路とをそれぞれ設
け、前記蒸気供給路の開閉弁を操作して蒸気圧を低圧及
び高圧の二段切り換えによって加熱処理するとともに、
各蒸気チャンバの蒸気並びに排出流体を抽出するように
している。
In the present invention, in order to achieve the above object, expandable thermoplastic resin particles are formed in a cavity formed with a male mold and a female mold provided with a steam chamber, or a female mold is formed so as to be able to approach and separate from each other. In the method of foaming and fusing by heating, the steam chamber in at least one of the male mold and the female mold is divided into a plurality of independent steam chambers, and an on-off valve is provided for each steam chamber. A steam supply path with a valve, a drain discharge path with an on-off valve, and a suction flow path connected to a vacuum pump further with an on-off valve are provided, and the on-off valve of the steam supply path is operated to reduce the steam pressure to low pressure and high pressure. Heat treatment by two-stage switching of
The steam in each steam chamber and the exhaust fluid are extracted.

なお、蒸気供給路の開閉弁が、操作流体供給路に介在
されたレギュレータで制御されるものであって、該レギ
ュレータの操作が、電空レギュレータを用い、コンピュ
ータよりの電圧指令により行われるものであることが好
ましい。
The on-off valve of the steam supply passage is controlled by a regulator interposed in the operation fluid supply passage, and the operation of the regulator is performed by a voltage command from a computer using an electropneumatic regulator. Preferably, there is.

また、雌金型が、リング状の周側部分の蒸気チャンバ
と、周側部分の一端部分を閉塞した蒸気チャンバとを個
別に区画して内部に凹状キャビティを形成したものであ
って、他端面部分に嵌合する雄金型を別の蒸気チャンバ
を持って備えたものであることが好ましい。
Further, the female mold is one in which a concave-shaped cavity is formed by separately dividing a ring-shaped steam chamber of a peripheral part and a steam chamber in which one end of the peripheral part is closed, and the other end face is formed. It is preferable that a male mold to be fitted to the portion is provided with another steam chamber.

また、蒸気供給工程が、開閉弁の弁開閉エアの圧力を
調節するレギュレータと減圧弁によって設定して行われ
得るものであることが望ましい。
Further, it is desirable that the steam supply step can be performed by setting with a regulator for adjusting the pressure of the valve opening / closing air of the on / off valve and a pressure reducing valve.

なお、各金型の加熱・放冷時に真空ポンプを用いて蒸
気チャンバ内の流体を吸引して真空状態下で加熱・放冷
すると良い。
When heating and cooling each mold, it is preferable that the fluid in the steam chamber is sucked using a vacuum pump and heated and cooled under vacuum.

〔作 用〕(Operation)

本発明によれば、先ず、成形金型を型閉めして金型内
のキャビティを真空にし、原料充填時にもエア充填せず
に真空下に原料充填した後、エアにて加圧した原料を補
充填した後にフローバックしてから金型を加熱し、その
後、真空作用を利用して金型内を真空にする。
According to the present invention, first, the molding die is closed and the cavity in the die is evacuated. After the supplemental filling, the mold is heated after flowing back, and then the inside of the mold is evacuated by utilizing the vacuum action.

次いで、一方の金型の独立した蒸気チャンバと他方の
金型の蒸気チャンバにスチーム圧力を例えば0.2kg/cm2G
以下の低圧で供給加熱し、一方の金型の独立した蒸気チ
ャンバと他方の金型の蒸気チャンバにスチーム圧力0.4k
g/cm2G以下の高圧で供給加熱し、一方の金型の独立した
残りの蒸気チャンバにスチーム圧力を例えば0.2kg以下
で供給加熱するとともに、一方の金型の残りの蒸気チャ
ンバにスチーム圧力を例えば0.4kg以下で供給加熱し、
本加熱してから真空タンクを用い400mHg以下に一気に型
内を真空にすることで、一次ガス抜きをし、さらに真空
ポンプのみで真空にする二次ガス抜きをする。
Next, a steam pressure of, for example, 0.2 kg / cm 2 G was applied to the independent steam chamber of one mold and the steam chamber of the other mold.
Supply and heat at the following low pressure, steam pressure 0.4k to the independent steam chamber of one mold and the steam chamber of the other mold
g / cm 2 G or less, and supply and heat at a high pressure of not more than 0.2 kg, and supply and heat, for example, a steam pressure of 0.2 kg or less to the independent steam chamber of one mold, and steam pressure to the remaining steam chamber of one mold. For example, supply heating at 0.4 kg or less,
After the main heating, the inside of the mold is evacuated at a stretch to 400 mHg or less using a vacuum tank, thereby evacuating the primary gas, and then evacuating the secondary gas by using only a vacuum pump.

次いで、水冷後、排水エアの冷却工程を経て、真空ポ
ンプで−700mmHg位に行う放冷を一段、又は二段以上行
って開型、離型するもので、サイクル的に10分以下で成
形でき、蒸気使用量も従来の1/2〜1/3、例えば20kg/シ
ョット以下で可能となる。
Then, after water cooling, through the cooling step of the drainage air, one stage or two or more stages of cooling to be opened and released by performing a cooling to about -700 mmHg with a vacuum pump, can be molded in less than 10 minutes in a cycle In addition, the amount of steam used can be reduced to 1/2 to 1/3 of the conventional amount, for example, 20 kg / shot or less.

上記加熱の際、一方加熱を高圧、低圧の二段スチーム
を使用するので、比較的高圧で発泡させるより低圧にて
ジワジワ発泡させた方が良いブロック成形できるし、し
かも、一方加熱は内部融着を行うもので両面加熱にて外
側を融着させ、良質なブロック製品を成形できるととも
に、ガス抜き工程では内部の発泡ガスを真空にして強制
的に脱ガスをはかり真空タンク等を使用し、一気に蒸気
チャンバ内を高真空にするガス抜きは−400mmHg以下が
最も良い。これは、一気に底真空にすると、真空力によ
りスチロールが外側に引張られ、額縁現象が発生し、外
と内の比重が異なってしまい、そのため、外が大(密度
が大)になり、ガスの通りが悪くなり、サイクルものび
てしまい良好なブロック製品もできないからである。
At the time of the above-mentioned heating, high-pressure, low-pressure two-stage steam is used for heating, so it is better to foam at a low pressure than to foam at a relatively high pressure. The outside is fused by heating on both sides to form a good quality block product.In the degassing process, the inside foaming gas is evacuated to a vacuum and degassed forcibly and a vacuum tank is used. The best way to degas the inside of the steam chamber to a high vacuum is -400 mmHg or less. This is because, when the bottom vacuum is applied at once, the styrene is pulled outward by the vacuum force, the frame phenomenon occurs, the specific gravity of the outside and the inside differ, and therefore the outside becomes large (the density is large) and the gas This is because the street becomes worse and the cycle becomes longer, so that a good block product cannot be produced.

いずれにしろ、金型の加熱のため、蒸気供給工程とし
ては。蒸気圧を底圧及び高圧の二段切換えにより加熱処
理するのが良い。
In any case, as a steam supply process for heating the mold. The heat treatment is preferably performed by switching the vapor pressure between a bottom pressure and a high pressure in two stages.

〔実施例〕〔Example〕

本発明の実施例を第1図〜2図を参照して説明する
と、通気孔のあるインナープレートで蒸気チャンバ11,1
2、13を形成した金型1、3とで雌型と雄型を一対とし
て成形型を構成し、雄雌は両型の間にキャビティ部5が
形成されるように接離自在に対向させた枠体にそれぞれ
取付けられていて各蒸気チャンバ11、12、13への加熱蒸
気源Sからの加熱蒸気を供給するための蒸気供給管21、
22、23を接続して設け、蒸気供給管21、22、23中にエア
源Pに連絡する調圧部4のある開閉弁31、32、33を介在
配備してある。
An embodiment of the present invention will be described with reference to FIGS. 1 and 2. Referring to FIGS.
The molds 1 and 3 on which the molds 2 and 13 are formed constitute a mold as a pair of a female mold and a male mold, and the male and female are opposed to each other so as to freely contact and separate so that a cavity 5 is formed between the molds. Steam supply pipes 21, which are attached to the respective frame bodies and supply heating steam from the heating steam source S to the steam chambers 11, 12, and 13, respectively.
On / off valves 31, 32, 33 having a pressure regulating unit 4 communicating with an air source P are interposed and provided in the steam supply pipes 21, 22, 23, respectively.

即ち、雌型、雄型の金型の少なくともいずれか一方、
又は両方の金型にある蒸気チャンバを複数に独立した蒸
気チャンバに区画し、各蒸気チャンバ毎に開閉弁31、3
2、33のある蒸気供給路と、ドレーン弁の開閉弁34、3
5、36のあるドレーン排出路24、25、26と、さらにバッ
キュウム弁の開閉弁37、38、39のある真空ポンプ40に連
なる吸引流路27、28、29とをそれぞれ設けて各開閉弁を
順次操作して雄金型及び雌金型個別に調圧しつつ供給さ
れる蒸気並びに排出される流体を調整抽出するようにし
てある。
That is, at least one of a female mold and a male mold,
Alternatively, the steam chambers in both molds are divided into a plurality of independent steam chambers, and the on-off valves 31 and 3 are provided for each steam chamber.
Steam supply path with 2, 33 and on-off valves 34, 3 for drain valves
Drain discharge paths 24, 25, 26 with 5, 36, and suction paths 27, 28, 29 connected to a vacuum pump 40 with open / close valves 37, 38, 39 of vacuum valves are further provided. By sequentially operating the male and female molds, the supplied steam and the discharged fluid are adjusted and extracted while adjusting the pressure individually.

開閉弁が蒸気供給管21、22、23に介在されたレギュレ
ータ20により制御されるものであって、レギュレータ20
の操作が、電空レギュレータを用い、コンピュータより
の電圧指令により行われるものを用いるのが良いが、必
要に応じ、開閉弁の操作が、調圧エアで行われるもので
あって、ダイヤフラムの調圧部に減圧弁と開閉用電磁弁
から調整された弁開閉エアと金型に連絡された二次側ス
チームと、レギュレータで調圧された調圧エアとのエア
圧のバランスの変動で行われるものでも良いし、さらに
は、開閉弁の弁開閉エアの圧力を調節するレギュレータ
20と減圧弁19により設定して行われ得るものでも良い。
The on-off valve is controlled by a regulator 20 interposed in the steam supply pipes 21, 22, and 23.
It is preferable to use an electropneumatic regulator and an operation that is performed by a voltage command from a computer.However, if necessary, the operation of the on-off valve is performed using pressure-adjusted air. It is performed by the fluctuation of the air pressure balance between the valve opening / closing air adjusted from the pressure reducing valve and the solenoid valve for opening and closing to the pressure part, the secondary steam connected to the mold, and the regulated air regulated by the regulator. Or a regulator that regulates the pressure of the valve opening / closing air of the on / off valve.
What can be set and performed by 20 and the pressure reducing valve 19 may be used.

本実施例では、雌金型が、リング状の周側部分の蒸気
チャンバ12と、周側部分の一端部分を閉塞した蒸気チャ
ンバ11とを個別に区画した金型で構成して内部に凹状キ
ャビティ5を形成したものであって、他端面部分に嵌合
する雄金型3を別の蒸気チャンバ13を持って備えたもの
を用いてあるが、雄雌型逆の構成としても良いし、両型
とも雌金型としても良い。
In the present embodiment, the female mold is constituted by a mold in which a steam chamber 12 of a ring-shaped peripheral part and a steam chamber 11 in which one end of the peripheral part is closed are individually partitioned, and a concave cavity is formed therein. 5 which is provided with a male mold 3 fitted to the other end face portion and having another steam chamber 13, the male and female molds may be reversed. The mold may be a female mold.

各金型1、3の加熱・放冷時に真空ポンプ40を用いて
蒸気チャンバ11、12、13内の流体を吸引して真空状態下
で加熱・放冷する。
When the molds 1 and 3 are heated and cooled, the fluid in the steam chambers 11, 12 and 13 is sucked using the vacuum pump 40 and heated and cooled under vacuum.

また、調圧部4はダイヤフラムを用い金型1、3から
の二次側スチームが導入されるように配管16で連結する
とともに、エア源Pに接続され、レギュレータ20のある
調圧エアの配管17と、弁開閉エアの供給用として電磁弁
18と源圧弁19のある配管15とをそれぞれ備え、加熱蒸気
供給管21、22、23を全開から全閉の範囲に亘って調整す
るようにし、この開閉弁31、32、33により供給される蒸
気を蒸気チャンバ11、12、13に供給するようにしてあ
る。この場合、各金型蒸気チャンバ部の蒸気圧に対応し
て空気圧装置から加圧空気を流出して行うのがよく、い
ずれにしても開閉弁31、32、33の操作が、バランスよく
行えるようにしてある。
Further, the pressure regulating unit 4 is connected by a pipe 16 using a diaphragm so that secondary steam from the molds 1 and 3 is introduced, is connected to an air source P, and is connected to a pressure regulating pipe having a regulator 20. 17 and solenoid valve for supplying valve opening / closing air
18 and a pipe 15 having a source pressure valve 19, respectively, so that the heating steam supply pipes 21, 22, and 23 are adjusted over a range from fully open to fully closed, and supplied by the on-off valves 31, 32, and 33. The steam is supplied to the steam chambers 11, 12, and 13. In this case, the pressurized air is preferably discharged from the pneumatic device in accordance with the steam pressure of each mold steam chamber section. It is.

レギュレータ20は、雄金型及び雌金型を個別にスチー
ム圧を調圧することができるように電空レギュレータを
用い、各配管17に配備し、コンピュータQの電圧指令又
は電流指令により自動調整し、遠隔操作も或いは手動に
て手元制御できるようにすることも選んでできるし、レ
ギュレータ20の調節で開閉弁31、32、33による開閉制御
で蒸気供給に脈動を与えるのが良い。また、必要に応じ
流量調整弁、或いは減圧弁を代用しても良い。
The regulator 20 uses an electropneumatic regulator so that the male mold and the female mold can individually adjust the steam pressure, is arranged in each pipe 17, and automatically adjusts according to a voltage command or a current command of the computer Q. Remote control or manual hand control can be selected, and the supply of steam is preferably pulsated by opening and closing control by the on-off valves 31, 32, and 33 by adjusting the regulator 20. Further, a flow control valve or a pressure reducing valve may be used as necessary.

なお、蒸気チャンバ11、12、13において、蒸気チャン
バ11、13が同一制御で蒸気チャンバ12とは別系列で制御
するのが有効であり、蒸気使用量も節減できて効果的な
加工作業が可能となる。また、これら各金型の蒸気チャ
ンバ内には、蒸気配管を内蔵し、蒸気の均一分布で金型
を均一加熱して処理する構成するのが効果的である。
In the steam chambers 11, 12, and 13, it is effective that the steam chambers 11 and 13 are controlled in the same manner and are controlled in a different system from the steam chamber 12, so that the amount of steam used can be reduced and effective machining operations can be performed. Becomes In addition, it is effective that a steam pipe is built in the steam chamber of each of the molds so that the molds are uniformly heated and processed with a uniform distribution of steam.

第1図例での成形方法を経時的に追ってみると、雄金
型、雌金型の型閉後、原料充填前に真空工程(45秒)、
原料充填(15秒)、補充填工程(15秒)、フローバック
(5秒)、金型加熱(5秒)一方加熱前真空(5秒)、
低圧一方加熱(19秒):スチーム圧0.1kg/cm2G、高圧一
方加熱(10秒):スチーム圧0.35kg/cm2G、低圧他方加
熱(15秒):スチーム圧0.1kg/cm2Gの後に本加熱(8
秒):スチーム圧0.35kg/cm2Gした。
When the molding method in the example of FIG. 1 is followed over time, a vacuum step (45 seconds) is performed after closing the male and female molds and before filling the raw materials.
Raw material filling (15 seconds), supplementary filling process (15 seconds), flow back (5 seconds), mold heating (5 seconds), vacuum before heating (5 seconds),
Low pressure one-side heating (19 seconds): steam pressure 0.1 kg / cm 2 G, high pressure one-side heating (10 seconds): steam pressure 0.35 kg / cm 2 G, low pressure other heating (15 seconds): steam pressure 0.1 kg / cm 2 G After the main heating (8
Second): Steam pressure was 0.35 kg / cm 2 G.

次いで、一次ガス抜き(−400mmHg)に40秒、二次ガ
ス抜き20秒かけた後、水冷(5秒)排水エア(5秒)、
放冷−1(5秒)及び放冷2(面圧0.1kg/cm2G)にて型
開、離型して製品重量8.1kgのブロック状発泡樹脂成形
品が得られ、従来方法より大幅なサイクル短縮化が可能
となった(サイク5分22秒)。なお、使用スチーム量は
約20kgであった。
Next, after 40 seconds for primary gas release (-400 mmHg) and 20 seconds for secondary gas release, water cooling (5 seconds) drain air (5 seconds),
The mold is opened and released with cooling -1 (5 seconds) and cooling 2 (surface pressure 0.1 kg / cm 2 G), and a block-shaped foamed resin molded product with a product weight of 8.1 kg is obtained. Cycle shortening (cycle 5:22). The amount of steam used was about 20 kg.

なお、図中6は、金型移動用の駆動部で、例えば、油
圧シリンダが用いられ、固定金型に対する可動金型とな
る。10は真空タンクで、開閉弁8のある配管9で真空ポ
ンプ40にバイパス配備されていて、必要に応じ設けられ
る。
In the figure, reference numeral 6 denotes a driving unit for moving the mold, for example, a hydraulic cylinder is used, which is a movable mold for the fixed mold. Reference numeral 10 denotes a vacuum tank, which is provided as required by a pipe 9 having an on-off valve 8 and is bypassed to the vacuum pump 40.

また、金型では型閉完了手前において固定側の金型に
対して移動フレームを含む可動側の蒸気チャンバ13にあ
る金型3を高速型閉から低速型閉に切換えるスローダウ
ン位置と、型閉完了位置、これは原料充填工程に移行さ
せる信号と、雌型内の製品をエジェクトピンなどで突き
落とすタイミングを制御する位置のエジェクト位置と、
型開完了手前において、低速型開から高速型開へ切換え
るチェンジ位置と型開完了位置、離型を行う場合の時の
型開き間隔を制御する位置などを設定して運転される。
Further, in the mold, before the mold closing is completed, the mold 3 in the movable steam chamber 13 including the moving frame with respect to the fixed mold is switched from a high-speed mold closing to a low-speed mold closing, and Completion position, this is the signal to shift to the raw material filling process, and the eject position of the position that controls the timing of pushing down the product in the female mold with the eject pin, etc.
Before the mold opening is completed, the operation is performed by setting a change position for switching from a low speed mold opening to a high speed mold opening, a mold opening completion position, a position for controlling a mold opening interval when performing mold release, and the like.

いずれにしても、コンピュータQにおいて、雄型、雌
型の金型を開閉自在に対向配備して型内成形する際に、
両金型の間隔を、型閉完了、クラッキング、エジェク
ト、型開完了のデータをアナログセンサで検出してアナ
ログ信号として入力してA/D変換器でデジタル信号に変
換し、データ処理部で内部固定データと比較処理して金
型を移動駆動するシリンダ又はモータなどの駆動部を或
いは各工程でのサイクル制御して金型の開閉操作と成形
加工を調整するようにしてある。
In any case, in the computer Q, when the male mold and the female mold are arranged opposite to each other in an openable and closable manner to perform in-mold molding,
The data of the mold closing, cracking, eject, and mold opening completion are detected by an analog sensor, input as an analog signal, converted to a digital signal by an A / D converter, and internally processed by a data processing unit. The opening / closing operation of the mold and the forming process are adjusted by controlling a driving unit such as a cylinder or a motor for moving and moving the mold by comparing the fixed data with the fixed data, or by performing cycle control in each process.

〔発明の効果〕〔The invention's effect〕

以上のように本発明によれば、雄金型及び雌金型中の
少なくともいずれか一方の金型にある蒸気チャンバを複
数に独立した蒸気チャンバに区画し、各蒸気チャンバ毎
に開閉弁のある蒸気供給路と、開閉弁のあるドレーン排
出路と、さらに開閉弁のある真空ポンプに連なる吸引流
路とをそれぞれ設け、蒸気供給路の開閉弁を操作して蒸
気圧を低圧及び高圧の二段切り換えによって加熱処理す
るとともに、各蒸気チャンバの蒸気並びに排出流体を抽
出するようにしているので、発泡成形サイクルの大幅な
短縮化が可能で使用する蒸気量も少なくて良質な製品加
工が円滑確実に行われ、しかも、ビーズのガス抜き作用
も容易にして融着成形サイクルを大幅に短縮化でき生産
性を著しく向上できるほか加熱蒸気の温度、調節も容易
で保守、保安も簡便であり、取扱い簡便で安価な簡略タ
イプのものとすることができる効果がある。
As described above, according to the present invention, the steam chamber in at least one of the male mold and the female mold is divided into a plurality of independent steam chambers, and each steam chamber has an open / close valve. A steam supply path, a drain discharge path with an on-off valve, and a suction flow path connected to a vacuum pump with an on-off valve are further provided, and the on-off valve of the steam supply path is operated to reduce the steam pressure to two stages, low pressure and high pressure. The heat treatment is performed by switching, and the steam and exhaust fluid in each steam chamber are extracted, so that the foam molding cycle can be significantly shortened, and the amount of steam used is small, and high-quality product processing is performed smoothly and reliably. In addition, the bead degassing action is facilitated, the fusion molding cycle can be greatly shortened, productivity can be significantly improved, and the temperature and adjustment of the heated steam are easy, and maintenance and security are simple. There, there is an effect that can be made handling of simple and inexpensive simplified type.

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

第1図は本発明の実施例の系統説明図、第2図は開閉弁
の一実施例の系統説明図である。 S……蒸気源、P……エア源、Q……コンピュータ、
1、3……金型、4……調圧部、5……キャビティ部、
11、12、13……蒸気チャンバ、21、22、23……蒸気供給
管、24、25、26……ドレン排出路、27、28、29……吸引
流路、31、32、33……開閉弁、34、35、36……開閉弁、
40……真空ポンプ。
FIG. 1 is a system explanatory diagram of an embodiment of the present invention, and FIG. 2 is a system explanatory diagram of one embodiment of an on-off valve. S: steam source, P: air source, Q: computer,
1, 3 ... mold, 4 ... pressure regulating section, 5 ... cavity section,
11, 12, 13 ... steam chamber, 21, 22, 23 ... steam supply pipe, 24, 25, 26 ... drain discharge path, 27, 28, 29 ... suction flow path, 31, 32, 33 ... On-off valve, 34, 35, 36 ... On-off valve,
40 ... Vacuum pump.

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】蒸気チャンバを備えた雄金型及び雌金型、
或いは雌金型同士を接離可能に対向させて形成するキャ
ビティ内において発泡性熱可塑性樹脂粒子を加熱して発
泡融着させる熱可塑性樹脂の発泡成形方法において、前
記雄金型及び雌金型中の少なくともいずれか一方の金型
にある蒸気チャンバを複数の独立した蒸気チャンバに区
画し、各蒸気チャンバ毎に開閉弁のある蒸気供給路と、
開閉弁のあるドレーン排出路と、さらに開閉弁のある真
空ポンプに連なる吸引流路とをそれぞれ設け、前記蒸気
供給路の開閉弁を操作して蒸気圧を低圧及び高圧の二段
切り換えによって加熱処理するとともに、各蒸気チャン
バの蒸気並びに排出流体を抽出するようにしたことを特
徴とする熱可塑性樹脂の発泡成形方法。
A male and female mold with a steam chamber;
Alternatively, in a method of foaming and molding a thermoplastic resin in which a foamable thermoplastic resin particle is heated and foamed and fused in a cavity formed by facing the female molds so as to be able to approach and separate from each other, the method comprises the steps of: A steam chamber in at least one of the molds is divided into a plurality of independent steam chambers, and a steam supply path having an on-off valve for each steam chamber;
A drain discharge path having an on-off valve and a suction flow path connected to a vacuum pump further having an on-off valve are provided, and the on-off valve of the steam supply path is operated to perform a heat treatment by switching the vapor pressure between low pressure and high pressure in two stages. And extracting steam and exhaust fluid from each of the steam chambers.
【請求項2】蒸気供給路の開閉弁が、操作流体供給路に
介在されたレギュレータで制御されるものであって、該
レギュレータの操作が、電空レギュレータを用い、コン
ピュータよりの電圧指令により行われるものである請求
項1記載の熱可塑性樹脂の発泡成形方法。
2. An on-off valve for a steam supply path is controlled by a regulator interposed in an operation fluid supply path. The regulator is operated by an electropneumatic regulator in response to a voltage command from a computer. The method for foaming and molding a thermoplastic resin according to claim 1, wherein
【請求項3】雌金型が、リング状の周側部分の蒸気チャ
ンバと、周側部分の一端面部分を閉塞した蒸気チャンバ
とを個別に区画して内部に凹状キャビティを形成したも
のであって、他端面部分に嵌合する雄金型を別の蒸気チ
ャンバを持って備えた請求項1又は2記載の熱可塑性樹
脂の発泡成形方法。
3. A female mold wherein a concave cavity is formed therein by separately dividing a steam chamber having a ring-shaped peripheral portion and a steam chamber having a closed one end portion of the peripheral portion. 3. The method of foaming thermoplastic resin according to claim 1, further comprising a male mold fitted to the other end face portion with another steam chamber.
【請求項4】蒸気供給工程が、開閉弁の弁開閉エアの圧
力を調節するレギュレータと減圧弁によって設定して行
われ得るものである請求項1、2、又は3記載の熱可塑
性樹脂の発泡成形方法。
4. The foaming of a thermoplastic resin according to claim 1, wherein the steam supply step can be performed by setting a regulator and a pressure reducing valve for adjusting the pressure of the valve opening and closing air of the opening and closing valve. Molding method.
【請求項5】各金型の加熱・放冷時に真空ポンプを用い
て蒸気チャンバ内の流体を吸引して真空状態下で加熱・
放冷する請求項2、3、又は4記載の熱可塑性樹脂の発
泡成形方法。
5. When heating and cooling each mold, the fluid in the steam chamber is sucked using a vacuum pump to heat and cool the mold under vacuum.
5. The foam molding method for a thermoplastic resin according to claim 2, wherein the thermoplastic resin is allowed to cool.
JP63100124A 1988-04-25 1988-04-25 Method for foaming thermoplastic resin Expired - Fee Related JP2602447B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63100124A JP2602447B2 (en) 1988-04-25 1988-04-25 Method for foaming thermoplastic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63100124A JP2602447B2 (en) 1988-04-25 1988-04-25 Method for foaming thermoplastic resin

Publications (2)

Publication Number Publication Date
JPH01271225A JPH01271225A (en) 1989-10-30
JP2602447B2 true JP2602447B2 (en) 1997-04-23

Family

ID=14265582

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63100124A Expired - Fee Related JP2602447B2 (en) 1988-04-25 1988-04-25 Method for foaming thermoplastic resin

Country Status (1)

Country Link
JP (1) JP2602447B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013159043A1 (en) * 2012-04-19 2013-10-24 Construction Research & Technology Gmbh Apparatus and system for expanding expandable polymeric microspheres
US9333685B2 (en) 2012-04-19 2016-05-10 AkzoNobel Chemicals International B.V. Apparatus and system for expanding expandable polymeric microspheres
US9365453B2 (en) 2012-04-19 2016-06-14 Construction Research & Technology Gmbh Admixture and method for freeze-thaw damage resistance and scaling damage resistance of cementitious compositions
US10640422B2 (en) 2013-12-06 2020-05-05 Construction Research & Technology Gmbh Method of manufacturing cementitious compositions

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5831722A (en) * 1981-08-20 1983-02-24 Daisen Kogyo:Kk Method of foam molding of synthetic resin and apparatus for foam molding

Also Published As

Publication number Publication date
JPH01271225A (en) 1989-10-30

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