Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6364294B2 - - Google Patents
[go: Go Back, main page]

JPS6364294B2 - - Google Patents

Info

Publication number
JPS6364294B2
JPS6364294B2 JP55021860A JP2186080A JPS6364294B2 JP S6364294 B2 JPS6364294 B2 JP S6364294B2 JP 55021860 A JP55021860 A JP 55021860A JP 2186080 A JP2186080 A JP 2186080A JP S6364294 B2 JPS6364294 B2 JP S6364294B2
Authority
JP
Japan
Prior art keywords
mold
molded product
skin
cooling
heating
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
JP55021860A
Other languages
Japanese (ja)
Other versions
JPS56117631A (en
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 filed Critical
Priority to JP2186080A priority Critical patent/JPS56117631A/en
Publication of JPS56117631A publication Critical patent/JPS56117631A/en
Publication of JPS6364294B2 publication Critical patent/JPS6364294B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、発泡成形品の製造方法に関するもの
である。 発泡成形品は、従来、発泡性熱可塑性樹脂粒子
の予備発泡したものを成形型に充填し、加熱、膨
脹を行つた後、急冷却を行ない成形品の内部膨脹
圧により変形を生じない充分な放冷時間を経た後
に成形型から製品を取出すことにより製造されて
いる。この方法においては、成形型を低温度→高
温度→低温度という加熱、冷却を繰返すので消費
エネルギーが非常に大きい難点がある。また急冷
却するので成形品表面に薄いスキン層が形成さ
れ、内部揮発分の逸散が妨害され放冷時間を長く
する必要があり、そのため一工程のサイクル時間
も非常に長くかかる欠点がある。また、特公昭54
−15301においては成形型に予備発泡粒子を充填
し、加熱して后、金型内部圧が高圧下で金型キヤ
ビテーの容積を増大させ、膨脹させた后、圧縮・
冷却する方法を提案しているが、この場合成形型
の内部圧力が高いので急激な開放は内部圧力が爆
発的に発散することになり非常に危険であり、而
も成形品は表面艶がなく、かつ成形品の構造体と
してのハリのない柔軟な成形品となる。 本発明における方法は、上記方法と本質的に異
なり、加熱膨脹融着後、キヤビテイー表面温度が
60℃以下に降下しないよう55〜80℃の高温水を使
用して徐冷した後、型開きして、成形品が残余の
内部膨脹圧で膨脹させ、再度型締を行なう事によ
り、残留揮発分を成形体より強制的に排出させ、
同時に成形型に接した成形体表面のビーズは内部
ビーズに比して硬化しているので此の圧縮圧と内
部圧により表面ビーズの間隙を更に狭め、緻密な
並列の配向性をもつ強靭な表皮を形成させること
が出来る。表皮強度と内部圧力のバランスが容易
に出来るため1サイクルの時間短縮が可能とな
り、工程は安全で、且つ成形品表面は艶があり、
かつハリのある成形品を得ることが出来る。この
ように、本発明は簡単な方法によつて従来法の欠
点を解消し得たものであつて、成形型の温度低下
が従来法にくらべ非常に少いので成形型の加熱エ
ネルギーが省力化できる。そして、成形に要する
1サイクル時間も短縮されるので従来法に比較し
て最有利経済的に発泡成形体を製造することがで
きる成形方法であるといえる。更に、本発明によ
り製造される成形品は、その表皮が厚くて強靭と
なるので物理的にも優れている。 本発明方法は、(1)冷却用の水は成形型と集水開
放バスを例えば高圧空により回流させ、成形型蒸
気室内に設置した多数の広角スプレーにより均一
に内型壁に吹き付けキヤビテイー表面温度60〜95
℃、好ましくは70〜85℃になるように吹き付け冷
却を行なう。好ましくは、5〜20秒吹付冷却す
る。又、回流高温水は蒸発又は飛散に減水した水
量のみ追加するので非常に少量、補給すればよ
い。(2)吹付完了後、成形型内に冷却水が残らない
様に圧空排水を行ない、冷却水の完全排出後、成
形型をたとえば5〜20mmの間隙まで型開きし、内
部成形品が金型間隙からはみ出さない程度の時
間、型開きを維持して、次に完全な型締を行な
う。型締め完了後、成形品が成形型開放後に変形
を生じない時間0〜15秒、好ましくは5〜10秒間
放置し、次いで型開きして成形品を取り出す事を
特徴とする連続自動成形機による発泡成形方法で
ある。以下、更に詳細説明する。 従来の成形工程においては、発泡性熱可塑性樹
脂粒子を予備発泡し、適当な養生時間通常24時間
〜48時間放置後、成形型に充填し、該原料を蒸気
等の加熱媒体により加熱膨脹させて粒子間が一体
に融着した後、例えば20℃の冷却水を成形型に放
出して急冷し、成形品の内部残留発泡ガスの膨脹
を停止させる事により成形型開放後、成形品の膨
脹変形を停止させる事が出来る。そして成形品内
部残留発泡ガス分が多い場合は、冷却水を成形型
内に放出する時間を長くする必要がある。また、
予備発泡ビースの内部残留発泡ガス分が少い場合
は成形時の加熱膨脹、粒子間の一体融着に要する
加熱エネルギーが多くなる。一方、成形型内の成
形品は、成形型の急冷却により成形型に接触して
いる成形品表面が硬化してスキン層となり内部残
留発泡ガスの発散を妨害し、しかも発泡体である
為、冷却効果が悪いので相当長時間の低温冷却を
必要とする。成形品の硬化した表皮部の強度が内
部残留発泡ガスの膨脹圧力より少ない場合は、成
形型キヤビテイー表面で膨脹圧力を支えている
為、その時成形型を開放すれば成形品は直ちに膨
脹変形する。又、冷却効果が進み表皮部の強度が
強化され残留発泡ガスの膨脹圧力とバランスする
か又は強度以下になつた時、成形型の開放が可能
となり成形品の膨脹変形を押える事が出来る。 本発明では、成形型を55〜80℃の高温水で冷却
して、成形型と成形品が接触する成形型表面温度
が60〜95℃、好ましくは70〜85℃になるように
し、次いで高温冷却水を圧空により排水し、成形
型を、開放する。成形品表面は柔軟性のある状態
で成型品内部残留発泡ガスの膨脹圧力で膨脹す
る。成形型を僅かに開いた後(好ましくは5〜20
mm)、再度型締めを行なう時、膨脹した成形品は、
成形型に押えられ内部残留発泡ガスを強制的に外
部に逸散させると同時に、成形型に接する発泡性
ビーズは規則的に並列に配向させ得る。又、内部
残留発泡ガスの強制排出により表皮部と内部の残
留発泡ガス分布差が生じ、内部は断熱圧縮により
再膨脹するため成形品表面に厚い層状の表皮を形
成する。そして、この強固な表皮部は、残留発泡
ガスの膨脹圧力とバランスするか、又は表皮部強
度が内部膨脹圧力より大となるためキヤビテイー
表面温度を高温のままで成形型を開放しても膨脹
変形を起こさない状態となる。但し、成形品は各
部分の厚みが異なるので、部分的な時間差を補正
する必要があり、型締め後、0〜15秒、好ましく
は5〜10秒放置した後、型開き・離型・取り出し
を行なう必要がある。 本発明によつて製造した成形否は、従来、公知
の方法によつて、得た成形品よりも緩衝性に富み
表面硬度もよく、しかも強度、融着が非常に秀れ
ている。又、成形サイクルも20〜30%短縮可能と
なり、成形型の温度降下が少ないので、連続自動
運転時の成形型加熱に要する蒸気等の加熱エネル
ギーも20〜30%省力化出来る効果がある。 成形型は、従来使用している成形型で特に問題
がない、しかし、キヤビテイー型、コアー型の接
触インロー部を長くして、予備発泡ビーズの充填
に支障のない構造の成形型であれば、更に本発明
の効果を高める事が出来る。 本発明の成形品としては、従来、成形している
魚箱、包装緩衝材一般、その他型物品全般に適用
して、従来品以上の機能を発揮する事が出来るた
め、薄肉化、外装材等の簡略化等コストダウン効
果が期待出来る。 本発明に使用する合成樹脂は、発泡ビーズ成形
に使用される発泡ポリスチレン樹脂、発泡ポリオ
レフイン樹脂等の、発泡ビーズ成形に使用される
総ての樹脂に適用出来る。 本発明の効果を列記すると次の通りである。 (1) 成形型の予備加熱が不用となり、又加熱・冷
却の温度巾が少ないので蒸気等加熱エネルギー
が省力化される。 (2) 成形品の残留揮発分を強制的に逸散させる
為、成形サイクルが非常に短縮される。 (3) 成形品の緩衝特性が良好となる。 (4) 成形品の表皮が、発泡ビーズの規則的な配向
性構造となるため表面硬度及びその他物性が向
上する。 (5) 従来成形型により、そのまま改良成形品を得
ることが出来る。 次に実施例を記載して本発明を説明する。 実施例 発泡自動成形機SC−10B(東洋機械金属株式会
社製)を使用し、魚箱(510mm×294mm×85mm)2
ケ取り成形型に於て、55倍に予備発泡したポリス
チレン発泡ビーズを成形型クラツキング3mmで充
填し、表1の条件により充填・加熱・冷却・排水
後、成形型を10mm開いて後、型締めを行ない、型
開・離型・成形品取り出しを行なつた。 比較例 実施例と同一の発泡成形機及び成形型を用いて
(クラツキング3mm)、成形型内に55倍予備発泡ポ
リスチレンビーズを充填して、表1の条件で成形
した。
The present invention relates to a method for manufacturing a foam molded article. Conventionally, foam molded products are produced by filling a mold with pre-foamed particles of expandable thermoplastic resin, heating and expanding them, and then rapidly cooling them to a sufficient temperature that the molded product will not be deformed due to the internal expansion pressure. It is manufactured by removing the product from the mold after it has been left to cool. This method has the disadvantage that it consumes a lot of energy because the mold is repeatedly heated and cooled from low temperature to high temperature to low temperature. In addition, because of the rapid cooling, a thin skin layer is formed on the surface of the molded product, which impedes the dissipation of internal volatile matter and requires a longer cooling time, resulting in the drawback that the cycle time for one step is extremely long. In addition, special public service in Showa 54
-15301, the mold is filled with pre-expanded particles, heated, the internal pressure of the mold increases the volume of the mold cavity under high pressure, and after expansion, compression and
We have proposed a cooling method, but in this case, the internal pressure of the mold is high, so rapid release will cause the internal pressure to radiate explosively, which is extremely dangerous, and the molded product will have a matte surface. , and a flexible molded product with no firmness as a structure of the molded product. The method of the present invention is essentially different from the above-mentioned method, in that after heating and expansion welding, the cavity surface temperature is
After slow cooling using high-temperature water at 55 to 80℃ to prevent the temperature from dropping below 60℃, the mold is opened, the molded product expands with the remaining internal expansion pressure, and the mold is clamped again to remove residual volatilization. forcibly discharged from the molded body,
At the same time, the beads on the surface of the molded product in contact with the mold are hardened compared to the internal beads, so this compression pressure and internal pressure further narrow the gap between the surface beads, creating a strong skin with dense parallel orientation. can be formed. Since the balance between skin strength and internal pressure can be easily achieved, one cycle time can be shortened, the process is safe, and the surface of the molded product is glossy.
Moreover, a molded product with firmness can be obtained. As described above, the present invention can solve the drawbacks of the conventional method using a simple method, and since the temperature drop in the mold is much smaller than in the conventional method, the heating energy for the mold can be saved. can. Furthermore, since the one cycle time required for molding is also shortened, it can be said that this molding method can produce foam molded articles in the most advantageous and economical way compared to conventional methods. Furthermore, the molded product produced according to the present invention has a thick and tough skin, and is therefore physically superior. The method of the present invention is as follows: (1) Cooling water is circulated between the mold and the water collection open bath using, for example, high-pressure air, and is uniformly sprayed onto the inner mold wall by a large number of wide-angle sprayers installed in the mold steam chamber to increase the cavity surface temperature. 60-95
℃, preferably 70 to 85℃. Preferably, spray cooling is performed for 5 to 20 seconds. Furthermore, since the circulating high-temperature water is added only in the amount of water that has been reduced due to evaporation or scattering, a very small amount only needs to be replenished. (2) After the spraying is completed, drain the mold with compressed air so that no cooling water remains in the mold, and after completely draining the cooling water, open the mold to a gap of, for example, 5 to 20 mm, so that the internal molded product is not in the mold. The mold is kept open for a sufficient amount of time so that it does not protrude from the gap, and then the mold is completely clamped. After the mold clamping is completed, the molded product is left for 0 to 15 seconds, preferably 5 to 10 seconds, so that no deformation occurs after the mold is opened, and then the mold is opened to take out the molded product. This is a foam molding method. A more detailed explanation will be given below. In the conventional molding process, expandable thermoplastic resin particles are pre-foamed, left for an appropriate curing time (usually 24 to 48 hours), then filled into a mold, and the raw material is heated and expanded using a heating medium such as steam. After the particles are fused together, cooling water at, for example, 20°C is released into the mold to rapidly cool the mold and stop the expansion of the foaming gas remaining inside the mold, thereby preventing expansion and deformation of the mold after the mold is opened. can be stopped. If there is a large amount of foaming gas remaining inside the molded product, it is necessary to lengthen the time for discharging the cooling water into the mold. Also,
When the residual foaming gas content inside the pre-foamed beads is small, the heating energy required for heating expansion during molding and integral fusion between particles increases. On the other hand, as the molded product inside the mold is rapidly cooled, the surface of the molded product in contact with the mold hardens and forms a skin layer, which prevents the internal residual foaming gas from dispersing. Since the cooling effect is poor, low-temperature cooling for a considerable period of time is required. If the strength of the hardened skin of the molded product is less than the expansion pressure of the internal residual foaming gas, the mold cavity surface supports the expansion pressure, so if the mold is opened at that time, the molded product will immediately expand and deform. In addition, when the cooling effect progresses and the strength of the skin increases and balances with the expansion pressure of the residual foaming gas or becomes lower than the strength, the mold can be opened and expansion deformation of the molded product can be suppressed. In the present invention, the mold is cooled with high-temperature water of 55 to 80 °C so that the mold surface temperature where the mold and the molded product come into contact is 60 to 95 °C, preferably 70 to 85 °C, and then The cooling water is drained using compressed air, and the mold is opened. The surface of the molded product expands in a flexible state due to the expansion pressure of the foaming gas remaining inside the molded product. After slightly opening the mold (preferably 5 to 20
mm), when the mold is clamped again, the expanded molded product will
While the foaming gas remaining inside the mold is forcibly dissipated to the outside, the expandable beads in contact with the mold can be oriented in parallel in a regular manner. Further, due to the forced discharge of the internal residual foaming gas, a difference in distribution of the residual foaming gas occurs between the skin and the interior, and the interior re-expands due to adiabatic compression, thereby forming a thick layered skin on the surface of the molded product. This strong skin balances the expansion pressure of the residual foaming gas, or the strength of the skin is greater than the internal expansion pressure, so even if the mold is opened while the cavity surface temperature remains high, it will not expand and deform. It will be in a state where it will not occur. However, since the thickness of each part of the molded product is different, it is necessary to compensate for the local time difference. It is necessary to do this. The molded product produced according to the present invention has better cushioning properties and surface hardness than molded products obtained by conventionally known methods, and has excellent strength and fusion bonding. In addition, the molding cycle can be shortened by 20 to 30%, and since the temperature drop in the mold is small, the heating energy required for heating the mold during continuous automatic operation, such as steam, can be reduced by 20 to 30%. As for the mold, there are no particular problems with conventional molds, but if the contact pilot part of the cavity mold and core mold is lengthened so that there is no problem in filling the pre-foamed beads, Furthermore, the effects of the present invention can be enhanced. The molded product of the present invention can be applied to conventionally molded fish boxes, packaging cushioning materials in general, and other molded articles in general, and can exhibit functions superior to conventional products. Cost reduction effects such as simplification can be expected. The synthetic resin used in the present invention can be applied to all resins used in foamed bead molding, such as foamed polystyrene resin and foamed polyolefin resin used in foamed bead molding. The effects of the present invention are listed below. (1) There is no need to preheat the mold, and the temperature range for heating and cooling is small, so heating energy such as steam is saved. (2) The molding cycle is greatly shortened because residual volatile matter in the molded product is forcibly dissipated. (3) The molded product has better cushioning properties. (4) The skin of the molded product has a regularly oriented structure of foamed beads, improving surface hardness and other physical properties. (5) Improved molded products can be obtained using conventional molds. Next, the present invention will be explained with reference to Examples. Example Using an automatic foam molding machine SC-10B (manufactured by Toyo Kikai Kinzoku Co., Ltd.), two fish boxes (510 mm x 294 mm x 85 mm) were prepared.
Fill the mold with 55 times pre-expanded polystyrene foam beads with mold cracking of 3 mm, and after filling, heating, cooling, and draining according to the conditions in Table 1, open the mold by 10 mm, and then close the mold. The mold was opened, the mold was released, and the molded product was removed. Comparative Example Using the same foam molding machine and mold as in the example (cracking 3 mm), the mold was filled with 55x pre-expanded polystyrene beads and molded under the conditions shown in Table 1.

【表】 実施例による成形品の表皮部は、第1図にみら
れるように粒子が規則的に並置された配向性を有
する強度の優れたものであつたが、比較例のもの
は、粒子の配向性は全くないものであつた。
[Table] As shown in Figure 1, the skin of the molded product according to the example had excellent strength and had particles arranged side by side regularly. There was no orientation at all.

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

第1図は、本発明による成形品(魚箱)の一例
の1部断面図である。 1……成形品表皮部、2……成形品内部。
FIG. 1 is a partial sectional view of an example of a molded product (fish box) according to the present invention. 1... Skin part of the molded product, 2... Inside of the molded product.

Claims (1)

【特許請求の範囲】[Claims] 1 成形型のキヤビテイーへ熱可塑性樹脂の予備
発泡粒子を充填し、蒸気等の加熱媒体により該粒
子を加熱、膨脹させて発泡成形品を得る方法にお
いて、予備発泡粒子を加熱、膨脹、融着させた
後、キヤビテイーの表面温度が60℃以下に降下し
ないように55〜80℃の高温水を使用して徐冷し、
排水し、次いで型開きを行ない、その状態を維持
した後、型締めし、しかる後に成形品を取出すこ
とを特徴とする発泡成形品の製造方法。
1. A method for obtaining a foamed molded product by filling the cavity of a mold with pre-expanded particles of a thermoplastic resin and heating and expanding the particles using a heating medium such as steam, in which the pre-expanded particles are heated, expanded and fused. After that, the surface temperature of the cavity is slowly cooled using high temperature water of 55 to 80℃ to prevent it from dropping below 60℃.
A method for producing a foamed molded product, which comprises draining water, then opening the mold, maintaining that state, clamping the mold, and then taking out the molded product.
JP2186080A 1980-02-23 1980-02-23 Foam molding and its manufacture Granted JPS56117631A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2186080A JPS56117631A (en) 1980-02-23 1980-02-23 Foam molding and its manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2186080A JPS56117631A (en) 1980-02-23 1980-02-23 Foam molding and its manufacture

Publications (2)

Publication Number Publication Date
JPS56117631A JPS56117631A (en) 1981-09-16
JPS6364294B2 true JPS6364294B2 (en) 1988-12-12

Family

ID=12066863

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2186080A Granted JPS56117631A (en) 1980-02-23 1980-02-23 Foam molding and its manufacture

Country Status (1)

Country Link
JP (1) JPS56117631A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58171924A (en) * 1982-04-02 1983-10-08 Honda Motor Co Ltd Foamed resin molded body

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5415301A (en) * 1977-07-04 1979-02-05 Osaka Gensokuki Seisakushiyo K Reduction gear with swivel for auger screw

Also Published As

Publication number Publication date
JPS56117631A (en) 1981-09-16

Similar Documents

Publication Publication Date Title
US2954589A (en) Method of molding expanded resins
HU180099B (en) Method for penoplastic material by means of injection mo
JPS6364294B2 (en)
JPS5947976B2 (en) foam mold
JPS6127175B2 (en)
JPH11509490A (en) Molding
JP3189377B2 (en) Molding method of foamed synthetic resin molded product
JPH09155906A (en) Molding method for bead foam plastic
US3328228A (en) Insulative decorative wall and ceiling board and method for producing same
JPS5928169B2 (en) Foam molding method
JPS60190335A (en) Manufacture of expanded resin molding
JP4678744B2 (en) Manufacturing method of recycled foamed resin block
JP3189305B2 (en) Molding method of foamed synthetic resin molded product
JPH10113942A (en) Method for producing foam
US3590105A (en) Method of manufacture of a foamed polystyrene body
JP3081722B2 (en) Method for producing foamed molded article in olefin resin mold
JP5192169B2 (en) Method for producing in-mold foam molding
JPH06278143A (en) Molding method for foamed synthetic resin moldings
JP3536875B2 (en) Foam molding method
JPS6222351Y2 (en)
JPH02292026A (en) Molding method of foam casting model
JP3274554B2 (en) Method for producing foam molded article having upright portion
JPS6315138B2 (en)
JPH1058474A (en) Manufacture of foam molding in polyolefin resin mold
JPH09254179A (en) Foamed synthetic resin molded object and its molding method