JPH0616905Y2 - Pre-expansion device for expandable thermoplastic resin particles - Google Patents

Pre-expansion device for expandable thermoplastic resin particles

Info

Publication number
JPH0616905Y2
JPH0616905Y2 JP1990042672U JP4267290U JPH0616905Y2 JP H0616905 Y2 JPH0616905 Y2 JP H0616905Y2 JP 1990042672 U JP1990042672 U JP 1990042672U JP 4267290 U JP4267290 U JP 4267290U JP H0616905 Y2 JPH0616905 Y2 JP H0616905Y2
Authority
JP
Japan
Prior art keywords
foaming
foaming tank
resin particles
thermoplastic resin
exhaust pipe
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 - Lifetime
Application number
JP1990042672U
Other languages
Japanese (ja)
Other versions
JPH044036U (en
Inventor
欣三 増田
利昭 武政
保 河合
和寛 常藤
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.)
Kaneka Corp
Original Assignee
Kaneka Corp
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 Kaneka Corp filed Critical Kaneka Corp
Priority to JP1990042672U priority Critical patent/JPH0616905Y2/en
Publication of JPH044036U publication Critical patent/JPH044036U/ja
Application granted granted Critical
Publication of JPH0616905Y2 publication Critical patent/JPH0616905Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は発泡性熱可塑性樹脂粒子の予備発泡装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a prefoaming device for expandable thermoplastic resin particles.

〔従来の技術と解決すべき課題〕[Conventional technology and problems to be solved]

発泡性熱可塑性樹脂粒子によって発泡成形品を製造する
のにあたり、通常、発泡性熱可塑性樹脂粒子を予め所定
の倍率にまで予備発泡させた後、その予備発泡粒子を型
内で発泡させて、発泡成形品を製造している。この発泡
性熱可塑性樹脂粒子を予備発泡させる方法には常圧発泡
方法と加圧発泡方法の2種類が提供されている。
In producing a foamed molded article from the expandable thermoplastic resin particles, usually, the expandable thermoplastic resin particles are pre-expanded to a predetermined ratio in advance, and then the pre-expanded particles are expanded in a mold to be expanded. Manufactures molded products. There are two types of methods for pre-expanding the expandable thermoplastic resin particles: a normal pressure foaming method and a pressure foaming method.

常圧発泡方法は発泡性熱可塑性樹脂粒子を大気圧の下で
予備発泡させる方法である。この常圧発泡装置は第9図
に示すように、発泡槽1の上部が大気に開放されてい
て、発泡槽1内の発泡性熱可塑性樹脂粒子を攪拌しなが
ら給気配管2から加熱蒸気を吹き込み、発泡性熱可塑性
樹脂粒子を加熱して発泡させるように構成されている。
常圧発泡装置は発泡槽1の内圧が大気圧であるため、発
泡槽1の構造に法律などによる特別の制約がなく、装置
の製造コストが安くつき、しかも発泡槽1内の清掃など
のためのマンホール扉3を大きくすることができるとい
う利点がある。ところが、発泡槽が大気に開放されてい
るため、発泡性熱可塑性樹脂粒子の加熱温度にむらが生
じて、発泡倍率にばらつきが生じるという問題があっ
た。特に、発泡倍率が低くなるほど、発泡倍率のばらつ
きが大きくなるという欠点があった。
The atmospheric pressure foaming method is a method of prefoaming expandable thermoplastic resin particles under atmospheric pressure. As shown in FIG. 9, in this atmospheric pressure foaming device, the upper part of the foaming tank 1 is open to the atmosphere, and while heating the expandable thermoplastic resin particles in the foaming tank 1, heated steam is supplied from the air supply pipe 2. It is configured to blow and heat the expandable thermoplastic resin particles to foam.
Since the internal pressure of the foaming tank 1 of the atmospheric foaming apparatus is atmospheric pressure, there are no special restrictions on the structure of the foaming tank 1, the manufacturing cost of the apparatus is low, and the inside of the foaming tank 1 is cleaned. There is an advantage that the manhole door 3 can be enlarged. However, since the foaming tank is open to the atmosphere, there is a problem in that the heating temperature of the expandable thermoplastic resin particles becomes uneven and the expansion ratio varies. In particular, the lower the expansion ratio, the greater the variation in the expansion ratio, which is a drawback.

一方、加圧発泡方法は発泡性熱可塑性樹脂粒子を加圧下
で予備発泡させる方法である。この加圧発泡装置は第1
0図に示すように、密閉構造の発泡槽4内で発泡性熱可
塑性樹脂粒子を攪拌しながら給気配管2から加圧下で加
熱蒸気を吹き込み、発泡性熱可塑性樹脂粒子を加熱して
発泡させるように構成されたものである。加圧発泡装置
は発泡性熱可塑性樹脂粒子の加熱温度にむらが少ないた
め、ほぼ均一な発泡倍率の予備発泡粒子が得られる。し
かも短時間で発泡させることができることから、近年に
おいては予備発泡装置の主流になりつつある。
On the other hand, the pressure foaming method is a method of prefoaming the expandable thermoplastic resin particles under pressure. This pressure foaming device is the first
As shown in FIG. 0, while stirring the expandable thermoplastic resin particles in the closed structure foaming tank 4, heated steam is blown from the air supply pipe 2 under pressure to heat and expand the expandable thermoplastic resin particles. It is configured as follows. Since the pressure-foaming device has less unevenness in the heating temperature of the expandable thermoplastic resin particles, pre-expanded particles having a substantially uniform expansion ratio can be obtained. Moreover, since it is possible to foam in a short time, in recent years, the pre-foaming device is becoming the mainstream.

ところが、加圧発泡装置は発泡槽4内の圧力を制御する
ために圧力計5を用いるとともに、給気配管2及び排気
配管6に調圧弁やあるいは電磁弁7を用いる必要があ
り、圧力制御のための装置にコストが高く付くという問
題があった。また、発泡槽4はその使用する圧力範囲に
よっては第一種圧力容器に該当することから、法律によ
って発泡槽4の構造上,使用上に制約が課せられ、製作
コストが高くなるという問題もあった。しかも、発泡槽
4は加圧容器としての構成上、法律の制約によってマン
ホール扉8を大きくすることができない。このため、同
一の加圧発泡装置でたとえば着色した樹脂粒子を用いて
予備発泡させる場合などにおいては特に、色変えなどに
おいて発泡槽4内を掃除する必要があるが、小さいマン
ホールを通して発泡槽4内を掃除をするのは非常に困難
であった。
However, the pressure foaming device needs to use the pressure gauge 5 to control the pressure in the foaming tank 4, and to use the pressure regulating valve or the solenoid valve 7 for the air supply pipe 2 and the exhaust pipe 6, which is a pressure control device. However, there is a problem in that the cost of the device is high. Further, since the foaming tank 4 corresponds to a first-class pressure vessel depending on the pressure range used, there is a problem that the law imposes restrictions on the structure and use of the foaming tank 4 and increases the manufacturing cost. It was Moreover, since the foaming tank 4 is configured as a pressure vessel, the manhole door 8 cannot be enlarged due to legal restrictions. For this reason, it is necessary to clean the inside of the foaming tank 4 when changing the color, for example, when pre-foaming using colored resin particles in the same pressure foaming device, but inside the foaming tank 4 through a small manhole. It was very difficult to clean.

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

そこで、本考案者らは加圧発泡装置の利点を活かした常
圧発泡装置を得るため鋭意研究を重ねた結果、本考案に
至った。
Therefore, the inventors of the present invention have conducted extensive studies to obtain an atmospheric pressure foaming device that takes advantage of the advantages of the pressure foaming device, and as a result, have arrived at the present invention.

本考案の要旨とするところは、攪拌装置を備えた密閉型
の発泡槽と、該発泡槽内に加熱媒体を吹き込む給気配管
と、該発泡槽内に吹き込まれた加熱媒体を排出する排気
配管とを備え、該発泡槽内に収納された所定量の発泡性
熱可塑性樹脂粒子を攪拌しつつ該発泡槽内に加熱媒体を
吹き込み、当該樹脂粒子を加熱膨張させて予備発泡させ
る予備発泡装置において、前記排気配管を介して前記発
泡槽を常時大気に開放させるとともに、排出気体に流出
抵抗を生じさせる流出抵抗手段を該排気配管に設け、該
発泡槽内が正圧に保たれるようにしたことにある。
The gist of the present invention is that a closed-type foaming tank equipped with a stirring device, an air supply pipe for blowing a heating medium into the foaming tank, and an exhaust pipe for discharging the heating medium blown into the foaming tank. In a pre-expansion device for blowing a heating medium into the foaming tank while stirring a predetermined amount of the expandable thermoplastic resin particles contained in the foaming tank and thermally expanding the resin particles for pre-foaming. The foaming tank is always opened to the atmosphere through the exhaust pipe, and the exhaust piping is provided with an outflow resistance means for generating an outflow resistance in the exhaust gas so that the inside of the foaming tank is kept at a positive pressure. Especially.

かかる本考案の発泡性熱可塑性樹脂粒子の予備発泡装置
において、前記流出抵抗手段として前記排気配管におけ
る配管抵抗又はオリフィス板、邪魔板若しくは抵抗体な
どを用いたことにある。
In the pre-expansion device for expandable thermoplastic resin particles of the present invention, a pipe resistance in the exhaust pipe or an orifice plate, a baffle plate or a resistor is used as the outflow resistance means.

〔作用〕[Action]

かかる本考案の発泡性熱可塑性樹脂粒子の予備発泡装置
によれば、発泡性熱可塑性樹脂粒子は密閉型の発泡槽内
で攪拌装置によって攪拌させられつつ、給気配管から吹
き込まれた加熱媒体によって加熱されて、予備発泡させ
られる。すなわち、給気配管から吹き込まれた加熱媒体
は密閉型の発泡槽内に充満して効率的に温度を上昇さ
せ、攪拌させられている発泡性熱可塑性樹脂粒子をほぼ
均一に加熱して発泡させた後、その加熱媒体は発泡性熱
可塑性樹脂粒子から発生した気体とともに排気配管から
排出させられる。排気配管にはバルブなどの配管を閉鎖
する機器は取り付けられておらず、排気配管を介して発
泡槽は常に大気に開放されていて、発泡槽内の圧力が高
圧にならないようにされている。一方、排気配管には排
出される気体に流出抵抗が生ずる流出抵抗手段が設けら
れていて、その流出抵抗によって発泡槽内の圧力が正圧
に保たれ発泡性熱可塑性樹脂粒子の均一な加熱に寄与さ
れる。
According to the pre-expansion device for expandable thermoplastic resin particles of the present invention, the expandable thermoplastic resin particles are agitated by the agitating device in the closed-type foaming tank while being heated by the heating medium blown from the air supply pipe. It is heated and prefoamed. That is, the heating medium blown from the air supply pipe is filled in the closed type foaming tank to raise the temperature efficiently, and the expandable thermoplastic resin particles being stirred are heated almost uniformly to foam. After that, the heating medium is discharged from the exhaust pipe together with the gas generated from the expandable thermoplastic resin particles. The exhaust pipe is not equipped with a device for closing the pipe such as a valve, and the foaming tank is always open to the atmosphere through the exhaust piping so that the pressure in the foaming tank does not become high. On the other hand, the exhaust pipe is provided with an outflow resistance means which causes an outflow resistance to the exhausted gas, and the outflow resistance keeps the pressure in the foaming tank at a positive pressure to uniformly heat the expandable thermoplastic resin particles. Be contributed.

〔実施例〕〔Example〕

次に、本考案の実施例を図面に基づいて詳しく説明す
る。
Next, an embodiment of the present invention will be described in detail with reference to the drawings.

第1図において、符号10は予備発泡装置における発泡
槽であり、発泡槽10には図示しない攪拌装置が設けら
れていて、発泡槽10内に供給された発泡性熱可塑性樹
脂粒子をほぼ均一に攪拌し混合し得るように構成されて
いる。また、発泡槽10には内部の掃除や修理,点検な
どのためにマンホールを備え、そのマンホールは扉12
によって閉じられている。このマンホール及びその扉1
2は圧力容器に用いられる円形のものである必要はな
く、図に示すように長方形状の扉12を用いることがで
きるので、発泡槽10内への出入りなどが容易にされて
いる。更に、発泡槽10は発泡させられた予備発泡粒子
を取り出すために取出し口を備え、その取出し口はシリ
ンダ14により開閉させられる扉16によって閉じられ
ており、発泡槽10は全体として密閉構造をなしてい
る。かかる発泡槽10の構造は高い内圧に耐え得る強度
を備えた耐圧構造を有する圧力容器として構成されてお
らず、通常の強度を有する容器として構成されている。
In FIG. 1, reference numeral 10 is a foaming tank in the pre-foaming device, and a stirring device (not shown) is provided in the foaming tank 10 so that the expandable thermoplastic resin particles supplied into the foaming tank 10 are substantially uniform. It is configured so that it can be stirred and mixed. Further, the foaming tank 10 is provided with a manhole for cleaning, repairing, inspecting the inside, and the manhole is a door 12
Is closed by. This manhole and its door 1
2 does not have to be a circular one used for a pressure vessel, and a rectangular door 12 can be used as shown in the figure, so that it is easy to enter and exit the foaming tank 10. Furthermore, the foaming tank 10 is provided with an outlet for taking out the expanded pre-expanded particles, and the outlet is closed by a door 16 which is opened and closed by a cylinder 14, so that the foaming tank 10 has a closed structure as a whole. ing. The structure of the foaming tank 10 is not configured as a pressure vessel having a pressure resistant structure having a strength capable of withstanding a high internal pressure, but is configured as a container having normal strength.

発泡槽10の下部には発泡槽10の内部に高温の水蒸気
などの加熱媒体を吹き込むための給気配管18が設けら
れていて、一定流量の加熱媒体を発泡槽10内に供給し
得るようにされている。一方、発泡槽10の上部には排
気配管20が設けられていて、その排気配管20の内径
は吹き込まれた加熱媒体と、その加熱媒体によって加熱
発泡させられた発泡性熱可塑性樹脂粒子の発泡剤から発
生した気体とを発泡槽10の内圧を高めずに充分排出し
得る大きさとされている。かかる大きさの内径からなる
排気配管20は図に示すように、発泡槽10の上部から
下方へかけて充分長い配管が架設されている。排気配管
20の長さはその排気配管20内を流出させられる気体
の流出抵抗によって、発泡槽10内の内圧がゲージ圧で
正圧に保たれるように設定される。発泡槽10内の内圧
はたとえば0.005〜0.04kg/cm2に設定すると良く、更に
好ましくは0.01〜0.03kg/cm2が例示され、よく多用され
る最も好ましいのは0.015kg/cm2程度前後の設定であ
り、少なくとも発泡槽10が第一種圧力容器として認定
されない圧力値が選定され、排気配管20の長さを調整
することによって発泡槽10の内圧が所定の圧力値に設
定される。
An air supply pipe 18 for blowing a heating medium such as high-temperature steam into the inside of the foaming tank 10 is provided in the lower portion of the foaming tank 10 so that a constant flow rate of the heating medium can be supplied into the foaming tank 10. Has been done. On the other hand, an exhaust pipe 20 is provided in the upper part of the foaming tank 10, the inner diameter of the exhaust pipe 20 is a blown heating medium, and a foaming agent for the expandable thermoplastic resin particles thermally foamed by the heating medium. The gas generated from the foaming tank 10 is of a size that can be sufficiently discharged without increasing the internal pressure of the foaming tank 10. As shown in the figure, the exhaust pipe 20 having an inner diameter of such a size has a sufficiently long pipe extending from the upper part to the lower part of the foaming tank 10. The length of the exhaust pipe 20 is set so that the internal pressure in the foaming tank 10 is maintained at a positive pressure as a gauge pressure due to the outflow resistance of the gas flowing out of the exhaust pipe 20. Internal pressure in the foam tank 10 may When set to, for example, 0.005~0.04kg / cm 2, more preferably is exemplified 0.01~0.03kg / cm 2, most preferably the commonly frequently used 0.015 kg / cm 2 about the front and rear This is a setting, and at least a pressure value at which the foaming tank 10 is not recognized as a first-class pressure vessel is selected, and the internal pressure of the foaming tank 10 is set to a predetermined pressure value by adjusting the length of the exhaust pipe 20.

かかる構成の予備発泡装置において、発泡槽10内に供
給された発泡性熱可塑性樹脂粒子は攪拌装置によって攪
拌されながら、給気配管18から吹き込まれた加熱媒体
により加熱され、発泡させられる。給気配管18から吹
き込まれた加熱媒体は密閉構造の発泡槽10内をほぼ均
一に充満して発泡槽10内の温度を効率的に且つ迅速に
上昇させ、温度むらがないように発泡性熱可塑性樹脂粒
子を加熱しつつ排気配管20から排出される。加熱媒体
によって加熱され発泡させられた発泡性熱可塑性樹脂粒
子から発生させられた気体は、加熱媒体とともに排気配
管20から排出される。排出される気体が長い排気配管
20内を通過するときに生ずる流出抵抗によって、発泡
槽10内の圧力はわずかに正圧の加圧状態に保たれ、温
度むらの少ない加熱発泡が確保されて、発泡倍率にむら
の少ないほぼ均一な粒径を備えた予備発泡粒子が得られ
る。
In the pre-foaming device having such a configuration, the expandable thermoplastic resin particles supplied into the foaming tank 10 are heated by the heating medium blown from the air supply pipe 18 while being stirred by the stirring device to be foamed. The heating medium blown from the air supply pipe 18 almost uniformly fills the foaming tank 10 having a closed structure to efficiently and quickly raise the temperature in the foaming tank 10 so that the foaming heat is generated so that there is no temperature unevenness. The plastic resin particles are heated and discharged from the exhaust pipe 20. The gas generated from the expandable thermoplastic resin particles that are heated and foamed by the heating medium is discharged from the exhaust pipe 20 together with the heating medium. Due to the outflow resistance generated when the discharged gas passes through the long exhaust pipe 20, the pressure in the foaming tank 10 is maintained at a slightly positive pressure and a heated foaming with little temperature unevenness is ensured. It is possible to obtain pre-expanded particles having a substantially uniform particle size with a small expansion ratio.

また、かかる予備発泡装置を作動させるのにあたり、発
泡槽10内の圧力を計測して制御しても良いが、そのよ
うな装置はコストがかかるので装備しなくてすめば好都
合である。本発明に係る予備発泡装置は正にこうした制
御を行う必要はなく、発泡槽10の内圧は排気配管20
における流出抵抗によって大気圧よりわずかに高い圧力
に維持される。
Further, in operating the pre-foaming device, the pressure in the foaming tank 10 may be measured and controlled, but such a device is costly, so it is convenient not to equip it. The pre-foaming device according to the present invention does not need to perform such control exactly, and the internal pressure of the foaming tank 10 is the exhaust piping
The outflow resistance at maintains a pressure slightly above atmospheric.

以上、本考案の実施例を詳述したが、本考案はその他の
形態でも実施することが可能である。
Although the embodiments of the present invention have been described in detail above, the present invention can be implemented in other forms.

たとえば、配管において流出抵抗は配管の長さに正比例
することから、第2図に示すように、排気配管22の一
部にU字状の配管24を設けて、配管24を排気配管2
2に対してスライドさせ排気配管22の長さを変えるこ
とによって流出抵抗を変えられるように構成しても良
い。これにより、発泡槽10内の圧力を変化させること
ができる。また、U字状の配管24に代えて蛇腹式の配
管を設け、その蛇腹式の配管の長さを変えて流出抵抗を
調節し得るように構成しても良い。
For example, since the outflow resistance in the pipe is directly proportional to the length of the pipe, a U-shaped pipe 24 is provided in a part of the exhaust pipe 22 as shown in FIG.
The outflow resistance may be changed by sliding with respect to 2 and changing the length of the exhaust pipe 22. Thereby, the pressure in the foaming tank 10 can be changed. Alternatively, a bellows type pipe may be provided in place of the U-shaped pipe 24, and the length of the bellows type pipe may be changed to adjust the outflow resistance.

また、配管の流出抵抗は曲がり管によって増加すること
から、第3図に示すように、排気配管26の一部に曲が
り管28を適宜個数介挿して、流出抵抗を高めるように
することも可能である。
Further, since the outflow resistance of the pipe is increased by the bent pipe, it is also possible to increase the outflow resistance by inserting an appropriate number of bent pipes 28 in a part of the exhaust pipe 26 as shown in FIG. Is.

更に、第4図に示すように、排気配管30にオリフィス
板32を挿入し得るように構成し、オリフィス板32の
オリフィスの大きさを適宜変更して排出気体の流出抵抗
を変え、発泡槽10の内圧を所望の正圧に保持し得るよ
うにしても良い。排気配管30に配設されるオリフィス
板32は1つに限らず、第5図に示すように2箇所以上
に、適宜挿入し得るように構成しても良い。
Further, as shown in FIG. 4, an orifice plate 32 is constructed so that it can be inserted into the exhaust pipe 30, and the size of the orifice of the orifice plate 32 is appropriately changed to change the outflow resistance of the exhaust gas. The internal pressure may be maintained at a desired positive pressure. The number of the orifice plate 32 provided in the exhaust pipe 30 is not limited to one, and may be appropriately inserted in two or more places as shown in FIG.

また、第6図に示すように、オリフィス板32に代えて
邪魔板34を排気配管36に挿入し得るようにし、邪魔
板34によって排気配管36内の排出気体の流れを遮
り、気体の流出抵抗を高めることも可能である。この邪
魔板34は1箇所にのみ配設しても良いが、第7図に示
すように、排気配管36中の複数箇所に設けても良い。
この場合、邪魔板34は排気配管36内の排出気体の流
れを交互に遮るように配設されるのが好ましい。
Further, as shown in FIG. 6, a baffle plate 34 can be inserted into the exhaust pipe 36 in place of the orifice plate 32, and the baffle plate 34 blocks the flow of exhaust gas in the exhaust pipe 36 to prevent gas outflow resistance. It is also possible to increase. The baffle plate 34 may be provided at only one place, but as shown in FIG. 7, it may be provided at a plurality of places in the exhaust pipe 36.
In this case, the baffle plate 34 is preferably arranged so as to alternately block the flow of the exhaust gas in the exhaust pipe 36.

その他、排気配管における排出気体の流出抵抗を高める
ために、第8図に示すように、板状あるいは棒状の抵抗
体38を排気配管40に挿入するように構成しても良
い。
Besides, in order to increase the outflow resistance of the exhaust gas in the exhaust pipe, as shown in FIG. 8, a plate-shaped or rod-shaped resistor 38 may be inserted into the exhaust pipe 40.

以上、例示したように排気配管の一部に曲がり管やオリ
フィス板、邪魔板、あるいは各種形状を備えた抵抗体な
どを介装させることによって排出気体の流出抵抗を高め
ることができる。これにより、発泡槽10内の圧力を大
気圧よりわずかに高い値で所望の値に調整することがで
き、しかも排気配管の長さを短くすることができる。
As described above, the outflow resistance of exhaust gas can be increased by interposing a bent pipe, an orifice plate, a baffle plate, or a resistor having various shapes in a part of the exhaust pipe. As a result, the pressure in the foaming tank 10 can be adjusted to a desired value at a value slightly higher than the atmospheric pressure, and the length of the exhaust pipe can be shortened.

排気配管に配設された曲がり管、オリフィス板、邪魔板
あるいは抵抗体又は排気配管の長さは予め発泡槽の内圧
が設定された後は固定されても良いが、発泡性熱可塑性
樹脂粒子の種類あるいは加熱媒体の温度や吹き込み量な
どに応じて、適宜設定し得るようにしても良い。
The length of the bent pipe, the orifice plate, the baffle plate or the resistor or the exhaust pipe arranged in the exhaust pipe may be fixed after the internal pressure of the foaming tank is set in advance, but the length of the expandable thermoplastic resin particles It may be appropriately set depending on the type, the temperature of the heating medium, the blowing amount, or the like.

その他、本考案はその趣旨を逸脱しない範囲内で、当業
者の知識に基づき種々なる改良、修正、変形を加えた形
態で実施することが可能である。
In addition, the present invention can be implemented in a form in which various improvements, modifications and variations are added based on the knowledge of those skilled in the art without departing from the spirit of the present invention.

〔考案の効果〕[Effect of device]

かかる本考案の予備発泡装置における排気配管は、発泡
槽に吹き込まれた加熱媒体とその加熱媒体によって加熱
発泡させられた発泡性熱可塑性樹脂粒子から発生した気
体を発泡槽の内圧を高めることなく充分に排出し得る大
きさとされ、しかも排気配管中にバルブなどの管路を遮
断する装置が用いられることなく、排出気体の流出抵抗
によって発泡槽内の圧力をゲージ圧で正圧に保つように
しているため、発泡槽は従来の常圧発泡槽と同様の構造
で構成することができる。すなわち、本考案に係る発泡
槽は第一種圧力容器ではないため、法律などによる構造
上の制約がなく、低コストで製造することができ、しか
もマンホールを大きくすることができることから、発泡
槽内部の掃除が容易になる。
The exhaust pipe in the pre-foaming device of the present invention is sufficiently equipped with the heating medium blown into the foaming tank and the gas generated from the expandable thermoplastic resin particles heat-foamed by the heating medium without increasing the internal pressure of the foaming tank. The size of the foaming tank is set to a positive pressure by the outflow resistance of the exhaust gas without the use of a device such as a valve to block the pipeline in the exhaust pipe. Therefore, the foaming tank can be configured with the same structure as the conventional atmospheric pressure foaming tank. That is, since the foaming tank according to the present invention is not a first-class pressure vessel, there is no structural restriction by law, it can be manufactured at low cost, and the manhole can be enlarged. Makes cleaning easier.

また、本考案に係る発泡槽は密閉構造であるため、外気
が流入することなく給気配管から吹き込まれた加熱媒体
は発泡槽内に充満して、効率的に且つ迅速に発泡槽内の
温度をほぼ均一に高めることができ、発泡倍率がほぼ一
定の予備発泡粒子を得ることが可能となり、もって発泡
倍率の高い発泡も可能となる。
In addition, since the foaming tank according to the present invention has a closed structure, the heating medium blown from the air supply pipe is filled into the foaming tank without the outside air flowing in, and the temperature in the foaming tank is efficiently and quickly increased. Can be increased almost uniformly, and pre-expanded particles having a substantially constant expansion ratio can be obtained, and foaming with a high expansion ratio is also possible.

更に、本考案に係る予備発泡装置は発泡槽内の圧力を計
測しつつその制御をする圧力制御が不必であるため、設
備費が安価で済むとともに制御機器の故障もなく、安定
した操業が可能となるなど、本考案は優れた効果を奏す
る。
Further, since the pre-foaming device according to the present invention does not require pressure control for measuring and controlling the pressure in the foaming tank, the equipment cost is low and there is no failure of the control equipment, and stable operation is possible. The present invention has an excellent effect.

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

第1図は本考案に係る発泡性熱可塑性樹脂粒子の予備発
泡装置を説明するための説明図である。第2図乃至第8
図はいずれも本考案に用いられる流出抵抗手段の他の実
施例を説明するための図であり、第2図は配管の長さを
可変にした例を示す要部断面図、第3図は曲がり管を用
いた例を示す要部説明図、第4図はオリフィス板を用い
た例を示す断面図、第5図は複数のオリフィス板を用い
た例を示す側面図、第6図は邪魔板を用いた例を示す断
面図、第7図は複数の邪魔板を用いた例を示す側面断面
図、第8図は抵抗体を用いた例を示す断面図である。 第9図は従来の常圧発泡槽を示す説明図であり、第10
図は従来の加圧発泡槽を示す説明図である。 10;発泡槽 12;マンホール扉 18;給気配管 20,22,26,30,36,40;排気配管 24;配管(流出抵抗手段) 28;曲がり管(流出抵抗手段) 32;オリフィス板(流出抵抗手段) 34;邪魔板(流出抵抗手段) 38;抵抗体(流出抵抗手段)
FIG. 1 is an explanatory view for explaining a pre-expansion device for expandable thermoplastic resin particles according to the present invention. 2 to 8
Each of the drawings is a view for explaining another embodiment of the outflow resistance means used in the present invention, FIG. 2 is a cross-sectional view of a main part showing an example in which the length of the pipe is variable, and FIG. FIG. 4 is a sectional view showing an example using a bent pipe, FIG. 4 is a sectional view showing an example using an orifice plate, FIG. 5 is a side view showing an example using a plurality of orifice plates, and FIG. FIG. 7 is a sectional view showing an example using a plate, FIG. 7 is a side sectional view showing an example using a plurality of baffle plates, and FIG. 8 is a sectional view showing an example using a resistor. FIG. 9 is an explanatory view showing a conventional atmospheric pressure foaming tank,
The figure is an explanatory view showing a conventional pressure foaming tank. 10; Foaming tank 12; Manhole door 18; Air supply pipe 20, 22, 26, 30, 36, 40; Exhaust pipe 24; Pipe (outflow resistance means) 28; Curved pipe (outflow resistance means) 32; Orifice plate (outflow Resistance means) 34; Baffle plate (outflow resistance means) 38; Resistor (outflow resistance means)

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】撹拌装置を備えた密閉型の発泡槽と、該発
泡槽内に加熱媒体を吹き込む給気配管と、該発泡槽内に
吹き込まれた加熱媒体を排出する排気配管とを備え、該
発泡槽内に収納された所定量の発泡性熱可塑性樹脂粒子
を撹拌しつつ該発泡槽内に加熱媒体を吹き込み、当該樹
脂粒子を加熱膨張させて予備発泡させる予備発泡装置に
おいて、前記排気配管を介して前記発泡槽を常時大気に
開放させるとともに、排出気体に流出抵抗を生じさせる
流出抵抗手段を該排気配管に設け、該発泡槽内が正圧に
保たれるようにしたことを特徴とする発泡性熱可塑性樹
脂粒子の予備発泡装置。
1. A closed type foaming tank provided with a stirring device, an air supply pipe for blowing a heating medium into the foaming tank, and an exhaust pipe for discharging the heating medium blown into the foaming tank. In a pre-foaming device for blowing a heating medium into the foaming tank while stirring a predetermined amount of the expandable thermoplastic resin particles contained in the foaming tank to heat-expand the resin particles for pre-foaming, the exhaust pipe The foaming tank is constantly opened to the atmosphere via the air outlet, and outflow resistance means for causing outflow resistance to the exhaust gas is provided in the exhaust pipe so that the inside of the foaming tank is maintained at a positive pressure. Pre-expansion device for expandable thermoplastic resin particles.
【請求項2】前記流出抵抗手段として前記排気配管にお
ける配管抵抗又はオリフィス板、邪魔板若しくは抵抗体
などを用いたことを特徴とする発泡性熱可塑性樹脂粒子
の予備発泡装置。
2. A pre-expansion device for expandable thermoplastic resin particles, wherein pipe resistance in the exhaust pipe or an orifice plate, a baffle plate, a resistor or the like is used as the outflow resistance means.
JP1990042672U 1990-04-22 1990-04-22 Pre-expansion device for expandable thermoplastic resin particles Expired - Lifetime JPH0616905Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1990042672U JPH0616905Y2 (en) 1990-04-22 1990-04-22 Pre-expansion device for expandable thermoplastic resin particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1990042672U JPH0616905Y2 (en) 1990-04-22 1990-04-22 Pre-expansion device for expandable thermoplastic resin particles

Publications (2)

Publication Number Publication Date
JPH044036U JPH044036U (en) 1992-01-14
JPH0616905Y2 true JPH0616905Y2 (en) 1994-05-02

Family

ID=31554420

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1990042672U Expired - Lifetime JPH0616905Y2 (en) 1990-04-22 1990-04-22 Pre-expansion device for expandable thermoplastic resin particles

Country Status (1)

Country Link
JP (1) JPH0616905Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5642459A (en) * 1979-09-14 1981-04-20 Iwatsu Electric Co Ltd Push-button dialing circuit

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5642459A (en) * 1979-09-14 1981-04-20 Iwatsu Electric Co Ltd Push-button dialing circuit

Also Published As

Publication number Publication date
JPH044036U (en) 1992-01-14

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