JPH0622927B2 - Foam molding method - Google Patents
Foam molding methodInfo
- Publication number
- JPH0622927B2 JPH0622927B2 JP1039022A JP3902289A JPH0622927B2 JP H0622927 B2 JPH0622927 B2 JP H0622927B2 JP 1039022 A JP1039022 A JP 1039022A JP 3902289 A JP3902289 A JP 3902289A JP H0622927 B2 JPH0622927 B2 JP H0622927B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- water
- vacuum
- mold
- foam
- 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
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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、加熱膨張処理された熱可塑性樹脂発泡体に対
して行う冷却を、水冷とバキューム冷却とによって行う
ようにした発泡体の成形方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a method for molding a foam, in which cooling is performed on a thermoplastic resin foam subjected to a heat expansion treatment by water cooling and vacuum cooling. It is about.
〔従来の技術〕 発泡体を成形するには、一般に、熱可塑性樹脂発泡粒子
を予備発泡させた予備発泡粒子を、固定側型と移動側型
とからなる成形型にて形成される型窩内へ加圧空気と共
に強制的に送り込んで充填する。そして、上記の固定側
型および移動側型に形成されているスチームチャンバを
介して型窩内にスチームを送り込んで前記の予備発泡粒
子を加熱膨張させた後、水冷、放冷などの冷却処理を施
して成形品としての熱可塑性樹脂発泡体を得ている。[Prior Art] Generally, in order to mold a foam, pre-expanded particles obtained by pre-expanding thermoplastic resin expanded particles are formed in a mold cavity formed by a mold including a stationary side mold and a moving side mold. Is forcedly sent together with pressurized air to fill. Then, after the steam is fed into the mold cavity through the steam chambers formed in the fixed side mold and the moving side mold to expand the pre-expanded particles by heat, cooling treatment such as water cooling and cooling is performed. This is applied to obtain a thermoplastic resin foam as a molded product.
従来の発泡体成形方法において、前述の冷却処理は、加
熱膨張処理の後に直ちに水冷を数秒間行い、その後に放
冷若しくはバキューム冷却を行うようにしていた。特
に、水冷を行った後にバキューム冷却を行う方法にあっ
ては、水冷や空冷を単独で行う場合に比べて冷却サイク
ルの短縮を図ることができると共に、多量の水を消費す
る水冷のみの方法に比べて発泡成形工場の立地条件とし
ても水使用の点をあまり配慮する必要がなくなるといっ
た利点を有している(特公昭61−23102号公報参
照)。In the conventional foam molding method, in the above-described cooling treatment, immediately after the heat expansion treatment, water cooling is performed for a few seconds, and then cooling or vacuum cooling is performed. In particular, in the method of performing vacuum cooling after performing water cooling, the cooling cycle can be shortened compared to the case of performing water cooling or air cooling alone, and only the method of water cooling that consumes a large amount of water is used. On the other hand, it has an advantage that it is not necessary to pay much attention to the use of water as a location condition of a foam molding factory (see Japanese Patent Publication No. 61-23102).
しかしながら、上記従来のように、加熱膨張処理の後に
直ちに水冷却を行ったのでは、成形品の表面が急激に冷
却されて表層部に表皮が形成されてしまう。このため、
加熱膨張処理直後の成形品内部に残留しているスチーム
や発泡ガスの発散が阻止され、水冷後のバキューム冷却
において、その冷却機能(水の気化による冷却機能)を
十分に引き出すことができず、冷却サイクルの短縮化が
阻害されるという欠点を有していた。その上、上記スチ
ームの発散阻止により成形品内部に水を含みがちとなる
ため、乾燥や熟成の短縮化が図れないという欠点も有し
ていた。However, if water cooling is performed immediately after the heat expansion treatment as in the above-mentioned conventional case, the surface of the molded article is rapidly cooled and a skin is formed on the surface layer portion. For this reason,
Dispersion of steam and foaming gas remaining inside the molded product immediately after the heat expansion treatment is prevented, and in the vacuum cooling after water cooling, its cooling function (cooling function by vaporizing water) cannot be sufficiently drawn out, It has a drawback that the shortening of the cooling cycle is hindered. In addition, since the steam tends to contain water due to the prevention of steam emission, there is a drawback that drying and aging cannot be shortened.
本発明に係る発泡体の成形方法は、上記の課題を解決す
るために、熱可塑性樹脂粒子を予備発泡した予備発泡粒
子を成形型の型窩内へ充填し、この予備発泡粒子を加熱
膨張させて熱可塑性樹脂発泡体を成形した後、これを冷
却して型窩内から取り出す発泡体の成形方法において、
少なくとも加熱膨張後の熱可塑性樹脂発泡体を水冷する
前に、バキューム冷却を行うようにしたことを特徴とし
ている。The method for molding a foam according to the present invention is, in order to solve the above problems, pre-expanded particles obtained by pre-expanding thermoplastic resin particles are filled into the mold cavity of the mold, and the pre-expanded particles are thermally expanded. After molding the thermoplastic resin foam by cooling, it is cooled and taken out from the mold cavity.
It is characterized in that vacuum cooling is performed at least before water-cooling the thermoplastic resin foam after being heated and expanded.
なお、少なくとも加熱膨張後の熱可塑性樹脂発泡体を水
冷する前に、バキューム冷却を行うのであるから、上記
の水冷時において引き続きバキューム冷却を行うこと
も、さらに、水冷が終了した後においてもバキューム冷
却を行うことも必要に応じて加えられるものである。Since at least the thermoplastic resin foam after heat-expansion is water-cooled before being water-cooled, vacuum cooling may be continuously performed at the time of water-cooling, and further, even after water-cooling is completed, vacuum cooling may be performed. It is also possible to add as necessary.
上記の構成によれば、水冷に先立ってバキューム冷却が
行われるため、加熱膨張処理直後の熱可塑性樹脂発泡体
(成形品)内部に残留しているスチーム(水)や発泡ガ
スはバキューム冷却による減圧にて円滑に発散されると
共に、このときの発散によって或る程度冷却されるた
め、その後の冷却を水冷により行っても急激な冷却とは
ならず、加熱膨張処理直後の成形品の表層部に表皮が形
成されるのを抑止することができる。これにより、冷却
サイクルの短縮化並びに成形品内部の含水率の低減、更
に、乾燥や熟成の短縮化を図ることができる。その上、
上記の水冷の後において更にバキューム冷却を行う(若
しくは最初のバキューム冷却から引き続いて行う)場合
においては、前述の通り、表皮形成が抑止されたことに
より当該バキューム冷却において、その冷却機能を十分
に発揮して冷却サイクルの短縮化をより一層促進するこ
とができると共に、成形品内部の含水率を更に低減し
て、乾燥や熟成を一層短縮化することが可能となる。According to the above configuration, since the vacuum cooling is performed before the water cooling, the steam (water) and the foaming gas remaining in the thermoplastic resin foam (molded product) immediately after the heat expansion treatment are decompressed by the vacuum cooling. In addition to the smooth divergence, the divergence at this time cools to a certain extent, so that even if the subsequent cooling is performed with water, the cooling does not become abrupt, and the surface layer of the molded product immediately after the heat expansion treatment is not cooled. The formation of the epidermis can be suppressed. As a result, the cooling cycle can be shortened, the water content inside the molded article can be reduced, and the drying and aging can be shortened. Moreover,
When vacuum cooling is further performed after the above water cooling (or it is continued from the first vacuum cooling), the cooling function is fully exerted in the vacuum cooling due to the inhibition of skin formation as described above. As a result, it is possible to further accelerate the shortening of the cooling cycle, further reduce the water content in the molded article, and further shorten the drying and aging.
本発明の一実施例を第1図および第2図に基づいて説明
すれば、以下を通りである。An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.
本発明に係る発泡体の成形方法において、第2図に示す
ように、この方法に用いられる発泡成形型1は、固定状
態に設けられた固定側型2と移動可能に設けられた移動
側型3とで構成されている。固定側型2の内部にはスチ
ームチャンバ4が、移動側型3にはスチームチャンバ5
・5′がそれぞれ形成されており、かつ、固定側型2と
移動側型3の各々の成形壁面にそれぞれ多数のコアベン
ト2a…、3a…が形成されていて、固定側型2と移動
側型3との型合わせにて形成される型窩6と上記スチー
ムチャンバ4・5・5′との間でスチームなどが通過で
きるようになっている。型窩6内に充填された予備発泡
粒子を加熱膨張させるための上記スチームは、図示しな
い導入管によって上記のスチームチャンバ4・5・5′
内に導かれるようになっている。また、スチームチャン
バ4・5内には、冷却水を噴出するためのノズル7・8
が各々の型2・3の上部から下方に向けて延設されてい
る。上記のノズル7・8は水冷弁9・10を介して冷却
水供給管11・12にそれぞれ連通されており、上記水
冷弁9・10の開閉によって、スチームチャンバ4・5
・5′内への冷却水の供給およびその停止が切り替わる
ようになっている。さらに、型2・3の下部には、スチ
ームチャンバ4・5内と図示しない真空(低圧)発生装
置との間を連通する連通管13・14がそれぞれ配され
ており、この連通管13・14に介設された真空弁15
・16によってスチームチャンバ4・5・5′内の真空
(低圧)状態および大気圧状態の切り替えが行われるよ
うになっている。また、前記の固定側型2には、熱可塑
性樹脂発泡粒子を予備発泡させた予備発泡粒子を前記の
型窩6内へ加圧空気と共に強制的に送り込んで充填する
ための原料充填器17が設けられている。In the method for molding a foam according to the present invention, as shown in FIG. 2, a foam molding die 1 used in this method includes a fixed side mold 2 provided in a fixed state and a movable side mold provided so as to be movable. 3 and 3. The stationary side mold 2 has a steam chamber 4 inside, and the movable side mold 3 has a steam chamber 5 inside.
5'is formed respectively, and a large number of core vents 2a ... 3a ... Are formed on the molding wall surfaces of the fixed mold 2 and the movable mold 3, respectively. Steam and the like can pass between the mold cavity 6 formed by mold matching with the mold 3 and the steam chambers 4, 5, 5 '. The steam for heat-expanding the pre-expanded particles filled in the mold cavity 6 is supplied to the steam chambers 4, 5, 5'by an introduction pipe (not shown).
It is designed to be guided inside. Further, nozzles 7 and 8 for ejecting cooling water are provided in the steam chambers 4 and 5.
Are extended downward from the upper part of each mold 2 and 3. The nozzles 7 and 8 are communicated with the cooling water supply pipes 11 and 12 via water cooling valves 9 and 10, respectively, and the steam chambers 4 and 5 are opened and closed by opening and closing the water cooling valves 9 and 10.
-The supply of cooling water into 5'and its stop can be switched. Further, communication pipes 13 and 14 for communicating between the inside of the steam chambers 4 and 5 and a vacuum (low pressure) generating device (not shown) are arranged below the molds 2 and 3, respectively. Vacuum valve 15 installed in
The switch 16 switches the vacuum (low pressure) state and the atmospheric pressure state in the steam chambers 4, 5, and 5 '. Further, the fixed side mold 2 is provided with a raw material charging device 17 for forcibly sending pre-expanded particles obtained by pre-expanding thermoplastic resin expanded particles into the mold cavity 6 together with pressurized air for filling. It is provided.
発泡体成形を行うには、原料充填器17にて型窩6内に
予備発泡粒子を充填した後、スチームチャンバ4・5・
5′を介して型窩6内にスチームを送り込んで予備発泡
粒子を加熱膨張させる。かかる工程は従来と同様であ
る。In order to perform the foam molding, after filling the pre-expanded particles in the mold cavity 6 with the raw material filling device 17, the steam chambers 4, 5, ...
Steam is fed into the mold cavity 6 through 5'to heat and expand the pre-expanded particles. Such steps are the same as conventional ones.
そして、この加熱膨張処理後における成形品Aの冷却に
おいて、この加熱膨張処理直後の冷却は、バキューム冷
却によって行う。バキューム冷却は、第1図(a)に示
すように、まず、水冷弁9・10を閉状態(図中の弁記
号において黒塗は閉状態、白抜きは開状態を示す)に保
持したまま真空弁15・16を開状態に切り替え、スチ
ームチャンバ4・5・5′内および型窩6内を真空状態
(減圧状態)にすることによって行う。なお、このバキ
ューム冷却における真空度は、300mmHg〜750mmHg
とするのが望ましい。次いで、同図(b)に示すよう
に、真空弁15・16を開状態に維持したまま、水冷弁
9・10を開状態に切り替え、ノズル7・8によってス
チームチャンバ4・5・5′を介して型窩6内に冷却水
を導入する。即ち、水冷とバキューム冷却とを同時併用
する。なお、この冷却時間は、成形品の形状や大きさ、
材質等によって適宜設定される。その後、同図(c)に
示すように、水冷弁9・10を閉状態に切り替え、スチ
ームチャンバ4・5・5′内および型窩6内への冷却水
の噴出を停止して、再びバキューム冷却のみを行う。こ
のような一連の冷却工程を経た後、同図(d)に示すよ
うに、真空弁15・16を閉状態に切り替え冷却サイク
ルを終了し、固定側型2と移動側型3との型開きを行っ
て成形品Aの取に出しを行う。In the cooling of the molded product A after the heat expansion treatment, the cooling immediately after the heat expansion treatment is performed by vacuum cooling. For vacuum cooling, as shown in FIG. 1 (a), first, while maintaining the water cooling valves 9 and 10 in a closed state (in the figure, the black symbol indicates a closed state, the white symbol indicates an open state). The vacuum valves 15 and 16 are switched to the open state, and the inside of the steam chambers 4, 5, and 5'and the inside of the mold cavity 6 are brought into a vacuum state (a reduced pressure state). The degree of vacuum in this vacuum cooling is 300 mmHg to 750 mmHg.
Is desirable. Next, as shown in FIG. 7B, the water cooling valves 9 and 10 are switched to the open state while the vacuum valves 15 and 16 are maintained in the open state, and the steam chambers 4, 5, and 5 ′ are opened by the nozzles 7 and 8. Cooling water is introduced into the mold cavity 6 through the mold. That is, water cooling and vacuum cooling are used together. The cooling time depends on the shape and size of the molded product,
It is appropriately set depending on the material and the like. After that, as shown in FIG. 7C, the water cooling valves 9 and 10 are switched to the closed state, the ejection of the cooling water into the steam chambers 4, 5 and 5'and the mold cavity 6 is stopped, and the vacuum is resumed. Only cool. After such a series of cooling steps, as shown in FIG. 3D, the vacuum valves 15 and 16 are switched to the closed state to end the cooling cycle, and the fixed side mold 2 and the moving side mold 3 are opened. Then, the molded product A is taken out.
上記の構成によれば、水冷に先立ってバキューム冷却が
行われるため、加熱膨張処理直後の成形品A内部に残留
しているスチーム(水)や発泡ガスはバキューム冷却に
よる減圧にて円滑に発散されると共に、このときの発散
によって或る程度冷却されるため、その後の冷却を水冷
により行っても急激な冷却とはならず、加熱膨張処理直
後の成形品の表層部に表皮が形成されるのを抑止するこ
とができる。これにより、冷却サイクルの短縮化並びに
成形品内部の含水率の低減、更に、乾燥や熟成の短縮化
を図ることができる。According to the above configuration, since the vacuum cooling is performed before the water cooling, the steam (water) and the foaming gas remaining inside the molded product A immediately after the heat expansion treatment are smoothly released by the reduced pressure by the vacuum cooling. At the same time, since it is cooled to some extent by the divergence at this time, rapid cooling does not occur even if the subsequent cooling is performed by water cooling, and a skin is formed on the surface layer portion of the molded product immediately after the heat expansion treatment. Can be suppressed. As a result, the cooling cycle can be shortened, the water content inside the molded article can be reduced, and the drying and aging can be shortened.
その上、本実施例のように、最初のバキューム冷却から
引き続いて水冷中および水冷後にもバキューム冷却を行
う場合においては、前述した通り、成形品の表皮形成が
抑止されたことによって、当該水冷中および水冷後のバ
キューム冷却において、その冷却機能を十分に発揮して
冷却サイクルの短縮化をより一層促進することができる
と共に、成形品内部の含水率を更に低減して、乾燥や熟
成を一層短縮化することが可能となる。Furthermore, as in the present example, when vacuum cooling is continuously performed during and after water cooling from the first vacuum cooling, as described above, the skin formation of the molded article was suppressed, and In vacuum cooling after water cooling, the cooling function can be fully exerted to further shorten the cooling cycle, and the moisture content inside the molded product can be further reduced to further shorten drying and aging. Can be converted.
なお、上記の実施例においては、最初のバキューム冷却
から引き続いて水冷中および水冷後においてもバキュー
ム冷却を行ったが、これに限らず、最初のバキューム冷
却の後には水冷のみ(大気圧下での水冷)を行ってその
水冷後に再びバキューム冷却を行うようにしてもよい。In the above example, the vacuum cooling was performed during and after water cooling after the first vacuum cooling, but the present invention is not limited to this, and only water cooling is performed after the first vacuum cooling (at atmospheric pressure). Water cooling) may be performed, and after that water cooling, vacuum cooling may be performed again.
本発明の成形方法により実際に成形品を得た場合と、従
来方法により成形品を得た場合とにおいて、そのトータ
ル成形時間および成形品の含水率を比較した。このとき
の条件は、以下に示す通りである。The total molding time and the water content of the molded product were compared between the case where the molded product was actually obtained by the molding method of the present invention and the case where the molded product was obtained by the conventional method. The conditions at this time are as shown below.
発泡成形機:ACE−12QS((株)積水工機製作所
製)。Foam molding machine: ACE-12QS (manufactured by Sekisui Machinery Co., Ltd.).
原料:ESD(積水化成品工業株式会社製)55倍予備
発泡粒使用(0.01kg/)。Raw material: ESD (manufactured by Sekisui Plastics Co., Ltd.) 55 times pre-expanded granules used (0.01 kg /).
成形品:外寸法450mm(縦)×350mm(横)×18
0mm(高さ)、最大厚み30mm。Molded product: External dimensions 450 mm (length) x 350 mm (width) x 18
0mm (height), maximum thickness 30mm.
以上は共通条件。The above are common conditions.
従来方法:水冷を5秒間行った後バキューム冷却(60
0mmHg)を75秒間行う。Conventional method: Water cooling for 5 seconds and vacuum cooling (60
0 mmHg) for 75 seconds.
実施例:バキューム冷却(500mmHg)を5秒間行った
後、大気圧下で水冷を5秒間行い、その後再びバキュー
ム冷却(600mmHg)を48秒間行う。Example: After vacuum cooling (500 mmHg) for 5 seconds, water cooling under atmospheric pressure for 5 seconds and then vacuum cooling (600 mmHg) for 48 seconds again.
以上の試験において、従来方法のトータル成形時間は1
05秒、実施例のそれは84秒であり、また、従来方法
により得られた成形品の含水率は5%、実施例のそれは
3.7%であった。従って、実施例の方法によれば、ト
ータル成形時間について21秒短縮されると共に、含水
率については1.3%低減された。In the above test, the total molding time of the conventional method is 1
05 seconds, that of the example was 84 seconds, the water content of the molded product obtained by the conventional method was 5%, and that of the example was 3.7%. Therefore, according to the method of the example, the total molding time was shortened by 21 seconds and the water content was reduced by 1.3%.
本発明に係る発泡体の成形方法は、以上のように、熱可
塑性樹脂粒子を予備発泡した予備発泡粒子を成形型の型
窩内へ充填し、この予備発泡粒子を加熱膨張させて熱可
塑性樹脂発泡体を成形した後、これを冷却して型窩内か
ら取り出す発泡体の成形方法において、少なくとも加熱
膨張後の熱可塑性樹脂発泡体を水冷する前に、バキュー
ム冷却を行うようにした構成である。As described above, the foam molding method according to the present invention is performed by filling the pre-expanded particles obtained by pre-expanding the thermoplastic resin particles into the mold cavity of the molding die and thermally expanding the pre-expanded particles to form the thermoplastic resin. After molding the foam, in the method of molding the foam which is cooled and taken out from the mold cavity, vacuum cooling is performed at least before water-cooling the thermoplastic resin foam after heat expansion. .
これにより、冷却サイクルを短縮してトータル成形時間
の短縮を図ることができると共に、成形品内部の含水率
を低減して、乾燥や熟成の短縮化も図ることができると
いう効果を奏する。As a result, the cooling cycle can be shortened to shorten the total molding time, and at the same time, the moisture content inside the molded product can be reduced to shorten the drying and aging.
第1図および第2図は本発明の一実施例を示すものであ
って、第1図(a)はバキューム冷却を行っている状態
を示す説明図、同図(b)はバキューム冷却と水冷とを
同時併用している状態を示す説明図、同図(c)はバキ
ューム冷却を行っている状態を示す説明図、同図(d)
は冷却工程を終了した状態を示す説明図、第2図は発泡
成形型の内部構造を示す断面図である。 1は発泡成形型、2は固定側型、3は移動側型、4・5
・5′はスチームチャンバ、6は型窩、7・8はノズ
ル、9・10は水冷弁、15・16は真空弁である。1 and 2 show an embodiment of the present invention. FIG. 1 (a) is an explanatory view showing a state where vacuum cooling is performed, and FIG. 1 (b) is a vacuum cooling and a water cooling. And (d) are explanatory views showing a state where and are simultaneously used, and (c) of the figure is an explanatory diagram showing a state of performing vacuum cooling, (d) of the same figure.
Is an explanatory view showing a state where the cooling step is finished, and FIG. 2 is a sectional view showing an internal structure of the foaming mold. 1 is a foam mold, 2 is a fixed mold, 3 is a movable mold, 4.5
5'is a steam chamber, 6 is a mold cavity, 7 is a nozzle, 9 is a water cooling valve, and 15 is a vacuum valve.
Claims (1)
粒子を成形型の型窩内へ充填し、この予備発泡粒子を加
熱膨張させて熱可塑性樹脂発泡体を成形した後、これを
冷却して型窩内から取り出す発泡体の成形方法におい
て、 少なくとも加熱膨張後の熱可塑性樹脂発泡体を水冷する
前に、バキューム冷却を行うことを特徴とする発泡体の
成形方法。1. A pre-expanded particle obtained by pre-expanding a thermoplastic resin particle is filled into a mold cavity of a mold, and the pre-expanded particle is thermally expanded to form a thermoplastic resin foam, which is then cooled. A method of molding a foam, which is characterized in that vacuum cooling is performed at least before water-cooling the thermoplastic resin foam after being heated and expanded, in the method of molding the foam taken out from the mold cavity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1039022A JPH0622927B2 (en) | 1989-02-17 | 1989-02-17 | Foam molding method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1039022A JPH0622927B2 (en) | 1989-02-17 | 1989-02-17 | Foam molding method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02217232A JPH02217232A (en) | 1990-08-30 |
| JPH0622927B2 true JPH0622927B2 (en) | 1994-03-30 |
Family
ID=12541487
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1039022A Expired - Lifetime JPH0622927B2 (en) | 1989-02-17 | 1989-02-17 | Foam molding method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0622927B2 (en) |
-
1989
- 1989-02-17 JP JP1039022A patent/JPH0622927B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02217232A (en) | 1990-08-30 |
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