[go: up one dir, main page]

JP3055831B2 - Foam molding method for foamed resin - Google Patents

Foam molding method for foamed resin

Info

Publication number
JP3055831B2
JP3055831B2 JP3299882A JP29988291A JP3055831B2 JP 3055831 B2 JP3055831 B2 JP 3055831B2 JP 3299882 A JP3299882 A JP 3299882A JP 29988291 A JP29988291 A JP 29988291A JP 3055831 B2 JP3055831 B2 JP 3055831B2
Authority
JP
Japan
Prior art keywords
mold
steam
heating
pressure
cavity
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
Application number
JP3299882A
Other languages
Japanese (ja)
Other versions
JPH05104649A (en
Inventor
義夫 白水
秀彦 山本
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.)
Toyo Machinery and Metal Co Ltd
Original Assignee
Toyo Machinery and Metal Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyo Machinery and Metal Co Ltd filed Critical Toyo Machinery and Metal Co Ltd
Priority to JP3299882A priority Critical patent/JP3055831B2/en
Publication of JPH05104649A publication Critical patent/JPH05104649A/en
Application granted granted Critical
Publication of JP3055831B2 publication Critical patent/JP3055831B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、発泡成形時間を大幅に
短縮する事の出来る発泡樹脂の発泡成形方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for foaming a foamed resin, which can greatly reduce the foaming time.

【0002】[0002]

【従来の技術】予備発泡粒を原料とした融着発泡成形で
現在最も汎用化されているものは発泡ポリスチレン (以
下EPSと略称)である。
2. Description of the Related Art Expanded polystyrene (hereinafter abbreviated as EPS) is one of the most widely used fusion foaming moldings using pre-expanded granules as a raw material.

【0003】EPSの内部融着を高める発泡方法として
は、真空加熱法や通流加熱法などがある。
[0003] As a foaming method for increasing the internal fusion of EPS, there are a vacuum heating method and a flow-through heating method.

【0004】前者の真空加熱法は、型閉めされた移動金
型と固定金型との間に形成されたキャビティ内に発泡樹
脂の予備発泡粒を充填し、移動金型及び固定金型それぞ
れの蒸気室内やキャビティ内の残留空気を真空により排
気せしめた後、一方側より他方に向けてキャビティ内に
おいて予備発泡粒間を高温蒸気が高圧で通流するように
0.3〜0.5kg/cm2程度の蒸気圧にて一方の金型から他方の
金型に向かって高温蒸気を所定時間通流させて、前記予
備発泡粒を急速に発泡成形させる通流加熱を行い、必要
により更に逆通流加熱をも行い、内部融着を促進させ
る。然る後、両金型の蒸気出口を閉じ、0.7〜0.8kg/cm2
の高圧蒸気圧にてキャビティ内の発泡成形体の表面を焼
き上げる両面加熱を行うというものである尚、成形品の
形状・厚さによっては通流加熱時に真空を利用して更に
内部融着を促進する場合もある。
In the former vacuum heating method, pre-expanded particles of foamed resin are filled in a cavity formed between a closed moving mold and a fixed mold, and each of the moving mold and the fixed mold is filled. After the residual air in the steam chamber and cavity is evacuated by vacuum, high-temperature steam flows between the pre-expanded particles in the cavity from one side to the other at high pressure.
A high-temperature steam is passed from one mold to the other mold at a steam pressure of about 0.3 to 0.5 kg / cm 2 for a predetermined time to carry out flow heating for rapidly foaming and molding the pre-expanded particles. If necessary, reverse flow heating is also performed to promote internal fusion. Thereafter, closing the steam outlet of the molds, 0.7~0.8kg / cm 2
The double-sided heating of baking the surface of the foam molded body in the cavity with high pressure vapor pressure is performed. Depending on the shape and thickness of the molded product, the internal fusion is further promoted by using a vacuum during flow heating. In some cases.

【0005】後者の通流加熱法は、型閉めされた移動金
型と固定金型との間に形成されたキャビティ内に発泡樹
脂の予備発泡粒を充填し、移動金型及び固定金型それぞ
れに高温蒸気を通して金型加熱を行い、然る後、キャビ
ティ内において予備発泡粒間を高温蒸気が高圧で通流す
るように0.3〜0.5kg/cm2程度の蒸気圧にて一方の金型か
ら他方の金型に向かって成形体内部のエアーを高圧蒸気
で追い出しつつ内部の加熱を促進し、必要により逆通流
加熱を行い、内部融着を促進した後、両金型の蒸気出口
を閉じ、通流加熱よりも更に高い圧力の蒸気でキャビテ
ィ内の発泡成形体の表面を焼き上げる両面加熱を行うと
いうものである。
In the latter flow-flow heating method, pre-expanded particles of a foamed resin are filled in a cavity formed between a closed moving mold and a fixed mold, and the moving mold and the fixed mold are individually charged. to perform mold heated through high-temperature steam, after which the one mold at 0.3~0.5kg / cm 2 about the vapor pressure as between the pre-expanded particle is high-temperature steam flowing in the high pressure in the cavity After expelling the air inside the compact with high-pressure steam toward the other mold, promote internal heating, perform reverse-flow heating as necessary, promote internal fusion, and then close the steam outlets of both molds. That is, double-sided heating in which the surface of the foam molded body in the cavity is baked with steam having a pressure higher than that of flow heating.

【0006】いずれの方法も、通流加熱工程でキャビテ
ィの予備発泡粒間に高温蒸気を通流させ、成形体の内部
融着を促進した後、通流加熱より更に高い圧力の蒸気で
両面加熱を行い、キャビティ内の発泡成形体の表面を焼
き上げ、成形体表面の成形状態が良好に仕上がるように
していた。
In either method, high-temperature steam is passed between the pre-expanded particles in the cavity in the flow heating step to promote internal fusion of the molded body, and then both sides are heated with steam at a higher pressure than the flow heating. Then, the surface of the foamed molded body in the cavity is baked, so that the molded state of the surface of the molded body is excellently finished.

【0007】しかしながらこれらの方法では、高い蒸気
圧により両面加熱時に高圧蒸気が成形体内に浸透し、断
熱材である成形体に加熱エネルギが内部にこもってしま
い、成形完了後の成形面圧の上昇を招き、金型内での十
分な冷却を行わないと成形体の変形を引き起こすという
問題がある。従って、前記加熱方法では、優れた発泡成
形体を製造する事が出来るものの冷却時間が長くなり、
それ故、発泡成形時間が長くなるという問題があった。
However, in these methods, high-pressure steam penetrates into the molded body due to the high vapor pressure when both sides are heated, and heating energy is trapped inside the molded body which is a heat insulating material. If the cooling in the mold is not performed sufficiently, there is a problem that the molded body is deformed. Therefore, in the heating method, although an excellent foam molded article can be produced, the cooling time becomes longer,
Therefore, there was a problem that the foam molding time was long.

【発明が解決しようとする課題】本発明の解決課題は、
成形体の面圧を低く抑える事によって発泡成形時間の短
縮を図る事にある。
The problem to be solved by the present invention is as follows.
An object of the present invention is to reduce the foam molding time by suppressing the surface pressure of the molded body.

【0008】[0008]

【課題を解決するための手段】そこで本発明発泡樹脂の
発泡成形方法では、 型閉めされた移動金型1と固定金型2との間に形成
されたキャビティ3内に発泡樹脂の予備発泡粒4を充填
し、 移動金型1及び固定金型2それぞれに高温蒸気を通し
て金型加熱を行い、 金型加熱の完了後キャビティ3内において予備発泡
粒4間を高温蒸気が高圧で通流するように0.8〜1.0kg/c
m2の蒸気圧にて一方の金型から他方の金型に向かって高
温蒸気を所定時間通流させて、前記予備発泡粒4を急速
に発泡成形させる通流加熱を行い、 然る後、両金型1,2の蒸気出口5,6を閉じ、0.
4〜0.5kg/cm2の蒸気圧にてキャビティ3内の発泡成形体
の表面を焼き上げる両面加熱を行う。 ;と言う技術的手段を採用した。
Accordingly, in the foam molding method of the present invention, the pre-expanded particles of the foamed resin are placed in the cavity 3 formed between the movable mold 1 and the fixed mold 2 whose molds are closed. 4 and high-temperature steam is passed through each of the movable mold 1 and the fixed mold 2 so that the high-temperature steam flows between the pre-expanded particles 4 in the cavity 3 at a high pressure after the completion of the mold heating. 0.8 ~ 1.0kg / c
At a vapor pressure of m 2 , high-temperature steam is passed from one mold to the other mold for a predetermined time to carry out flow heating for rapidly foaming and forming the pre-expanded granules 4. Close the steam outlets 5 and 6 of both molds 1 and 2 and
A double-sided heating for baking the surface of the foam molded body in the cavity 3 with a vapor pressure of 4 to 0.5 kg / cm 2 is performed. The technical means of;

【0009】これにより、通流加熱と両面加熱時の加熱
エネルギ差がなく、高エネルギが浸透する事もないの
で、成形体の面圧の上昇を招くことがなく、金型内での
成形体の冷却時間を大幅に短くする事が出来、以て発泡
成形時間の短縮を達成する事ができた。
[0009] Thus, there is no difference in heating energy between flow heating and double-side heating, and high energy does not penetrate, so that the surface pressure of the molded body does not increase, and the molded body in the mold does not rise. The cooling time can be greatly shortened, thereby shortening the foaming molding time.

【0010】[0010]

【実施例】以下、本発明を図示実施例に従って詳述す
る。図1は発泡成形機の主要部の概略断面図で、固定金
型2が固定ダイプレート7に装着されており、固定ダイ
プレート7の4隅に取り付けられたタイバー8に移動ダ
イプレート9が往復摺動自在に装着されており、この移
動ダイプレート9に移動金型1が装着されている。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. FIG. 1 is a schematic cross-sectional view of a main part of a foam molding machine. A fixed die 2 is mounted on a fixed die plate 7, and a movable die plate 9 reciprocates on tie bars 8 attached to four corners of the fixed die plate 7. The movable die 1 is mounted on the movable die plate 9.

【0011】更に、移動金型1の背部においてタイバー
8の端部にシリンダプレート10が装着されており、シリ
ンダダイプレート10に装着された駆動シリンダ11にて移
動ダイプレート9が移動金型1と共に往復運動するよう
になっている。固定金型2の背面には予備発泡粒4をキ
ャビティ3に供給するためのフィラー12が装着されてお
り、フィラー12には予備発泡粒4を貯蔵しているホッパ
13が接続されている。
Further, a cylinder plate 10 is mounted on the end of the tie bar 8 at the back of the movable die 1, and the movable die plate 9 is moved together with the movable die 1 by a driving cylinder 11 mounted on the cylinder die plate 10. It is designed to reciprocate. A filler 12 for supplying the pre-expanded particles 4 to the cavity 3 is mounted on the back surface of the fixed mold 2, and a hopper storing the pre-expanded particles 4
13 is connected.

【0012】次に金型1,2の構造について説明する。
金型1,2は固定側も移動側も同様で、ダイプレート7,
9に装着される金型本体1a,2aと、キャビティ3を構成
する雄型1bと雌型2bと、中空部分が蒸気室1d,2dとなっ
ており、金型本体1a,2aには蒸気配管14a,14bと蒸気出口
であるドレン弁5,6を有するドレン配管5a,6aとが接続
されている。雌、雄型1b,2bには蒸気噴出小孔1e,2eが多
数穿孔されており、金型1,2内に導入された蒸気が前
記蒸気噴出小孔1e,2eを通ってキャビティ3内に噴出(又
は通過)するようになっている。
Next, the structure of the dies 1 and 2 will be described.
The molds 1 and 2 are the same on both the fixed side and the movable side.
The mold bodies 1a and 2a mounted on the mold 9, the male mold 1b and the female mold 2b constituting the cavity 3, and the hollow portions are steam chambers 1d and 2d. Drain pipes 5a and 6a having drain valves 5 and 6 serving as steam outlets are connected to each other. The female and male molds 1b, 2b are provided with a large number of steam ejection holes 1e, 2e, and the steam introduced into the dies 1, 2 passes through the steam ejection holes 1e, 2e into the cavity 3. It gushes (or passes).

【0013】蒸気供給源15から導出された蒸気配管14は
途中で4本に分岐しており、そのうちの2本がペアとな
っていて、それぞれに高圧蒸気弁16a,16bと低圧蒸気弁1
7a,17bが接続されている。高圧蒸気弁16a,16bと低圧蒸
気弁17a,17bの出口では、高圧蒸気弁16aと低圧蒸気弁17
aが合流して分岐配管14aに接続し、雄金型1に接続され
ている。一方、高圧蒸気弁16bと低圧蒸気弁17bは、合流
して分岐配管14bに接続し、雌金型2に接続されてい
る。
The steam pipe 14 led out of the steam supply source 15 is branched into four pipes on the way, two of which are paired, each having a high-pressure steam valve 16a, 16b and a low-pressure steam valve 1 respectively.
7a and 17b are connected. At the outlets of the high-pressure steam valves 16a, 16b and the low-pressure steam valves 17a, 17b, the high-pressure steam valve 16a and the low-pressure steam valve 17
a are merged, connected to the branch pipe 14a, and connected to the male mold 1. On the other hand, the high-pressure steam valve 16b and the low-pressure steam valve 17b are merged and connected to the branch pipe 14b, and are connected to the female mold 2.

【0014】分岐配管14aには蒸気室1d内の蒸気圧力を
表示するための圧力計18が装備されている。この圧力計
18は、圧力設定装置付きで、蒸気室1d内の蒸気圧力が設
定圧力に達した時に高圧蒸気弁16aを閉じるように働
く。
The branch pipe 14a is provided with a pressure gauge 18 for indicating the steam pressure in the steam chamber 1d. This pressure gauge
Reference numeral 18 is provided with a pressure setting device and functions to close the high-pressure steam valve 16a when the steam pressure in the steam chamber 1d reaches the set pressure.

【0015】而して、駆動シリンダ11を作動して金型
1,2間に予備発泡粒4が飛び出さない程度の隙間をあ
けて型閉めを行い、フィラー12を作動させてキャビティ
3内に発泡樹脂の予備発泡粒4を充填する。空送エアー
は両金型間の間隙から流出する。
The drive cylinder 11 is operated to close the mold with a gap between the molds 1 and 2 such that the pre-expanded granules 4 do not protrude, and the filler 12 is actuated into the cavity 3. The pre-expanded particles 4 of the foamed resin are filled. The pneumatic air flows out of the gap between the two dies.

【0016】移動金型1及び固定金型2のドレン弁5,
6を開放し、かつ、両方の高圧蒸気弁16a,16bを開いて
金型1,2それぞれに高温蒸気を大流量で通して蒸気室1
d,2d内の空気を排出するための金型加熱を行う。
The drain valve 5 of the movable mold 1 and the fixed mold 2
6 is opened, and both high-pressure steam valves 16a and 16b are opened to allow high-temperature steam to flow through the molds 1 and 2 at a large flow rate.
Heat the mold to discharge the air in d and 2d.

【0017】金型加熱が完了すると、蒸気室1dのドレー
ン弁5を閉じ、蒸気室2dのドレーン弁6を開いた状態で
高圧蒸気弁16aを全開し(この時、他の高圧蒸気弁16bは
閉じられている。)、大流量の蒸気を蒸気室1dからキャ
ビティ3に充填された予備発泡粒4の隙間を通って蒸気
室2dに通流させ、然る後、ドレーン弁6を通して放出す
る。
When the heating of the mold is completed, the drain valve 5 of the steam chamber 1d is closed, and the high-pressure steam valve 16a is fully opened with the drain valve 6 of the steam chamber 2d open (at this time, the other high-pressure steam valve 16b is A large amount of steam is allowed to flow from the steam chamber 1d through the gap of the pre-expanded particles 4 filled in the cavity 3 to the steam chamber 2d, and then discharged through the drain valve 6.

【0018】キャビティ2内の予備発泡粒4の加熱膨張
に応じて蒸気室1d内を通流する時の抵抗としての通流蒸
気圧が上昇し、前記接点付きの圧力計18の指示値も上昇
してくる。通流蒸気圧が圧力計18の設定値に達したとこ
ろで、圧力計18が作動し、高圧蒸気弁16aを閉じて通流
加熱を完了する。又、必要により逆通流加熱を行い、通
流加熱完了とすることもある。本発明では上記の通流蒸
気圧は例えば0.8〜1.0kg/cm2(通常は1.0kg/cm2が使用さ
れる)と高く設定してある。これにより、予備発泡粒4
の中心まで熱を急速に伝えて内部融着を促進する。
In accordance with the thermal expansion of the pre-expanded particles 4 in the cavity 2, the flowing steam pressure as a resistance when flowing through the steam chamber 1d increases, and the indicated value of the pressure gauge 18 with the contact also increases. Will come. When the flowing steam pressure reaches the set value of the pressure gauge 18, the pressure gauge 18 is operated, the high-pressure steam valve 16a is closed, and the flowing heating is completed. If necessary, reverse flow heating may be performed to complete the flow heating. In the present invention it is flowing vapor pressure above set higher, for example 0.8~1.0kg / cm 2 (typically 1.0 kg / cm 2 is used). Thereby, the pre-expanded particles 4
Heat is rapidly transmitted to the center of the steel to promote internal fusion.

【0019】このようにして通流加熱が終了すると、開
放していたドレン弁6も閉じ(ドレーン弁5は最初から
閉じられている。)、かつ、両方の高圧蒸気弁16a,16bを
閉じ、代わりに低圧蒸気弁17a,17bを両方とも開いて発
泡成形体4aを両面から加熱し、発泡成形体4aの表面の焼
き上げを行う両面加熱工程に入る。両面加熱のときの蒸
気室1d,2dの蒸気圧は0.4〜0.6kg/cm2(通常は0.5kg/cm2
程度)で良い。両面加熱の加熱時間はタイマ規制で行わ
れる。上記両面加熱は、成形体4aの表面の融着を促進す
るものである。即ち、金型1,2の温度は金型加熱や通
流加熱によって加熱されているが、なお成形体4aより低
温であるため、成形体4aの表面は金型1,2に熱を奪わ
れ、内部に比べて融着が若干悪くなる。そこで、前記両
面加熱により、成形体4aの表面の融着を内部の融着と同
程度にするのである。
When the flow heating is completed in this manner, the drain valve 6 which has been opened is also closed (the drain valve 5 is closed from the beginning), and both high-pressure steam valves 16a and 16b are closed. Instead, both of the low-pressure steam valves 17a and 17b are opened to heat the foam molded body 4a from both sides, and a double-side heating step of baking the surface of the foam molded body 4a is started. Sided steam chamber 1d, the vapor pressure of 2d when the heating 0.4~0.6kg / cm 2 (typically 0.5 kg / cm 2
Degree). The heating time for double-sided heating is controlled by a timer. The double-sided heating promotes fusion of the surface of the molded body 4a. That is, although the temperatures of the molds 1 and 2 are heated by mold heating or flowing heating, since the temperature is lower than that of the molded body 4a, the surface of the molded body 4a is deprived of heat by the molds 1 and 2. , The fusion is slightly worse than inside. Thus, by the above-mentioned double-sided heating, the fusion of the surface of the molded body 4a is made almost the same as the fusion inside.

【0020】換言すれば、この両面加熱工程で、低圧蒸
気を少量だけキャビティ両面から与えるのは、通流加熱
工程で既にキャビティ内部の成形体は大流量高圧蒸気で
一様に加熱されて内部の発泡融着は殆ど完了しており、
ここでは成形体のキャビティ壁に近い表面部分の加熱不
均一を調整するだけでよく、成形体の外観仕上げのため
だけであるから、ごく短時間でよいことになる。この工
程で、従来のような高圧蒸気を大量にキャビティ両面か
ら与える必要は通流加熱の工程により既になくなってい
るし、これにより却って成形面圧を高くして次の冷却サ
イクルタイムを長くしてしまうだけで不利である。
In other words, the reason why a small amount of low-pressure steam is supplied from both sides of the cavity in this double-sided heating step is that the compact inside the cavity has already been uniformly heated by the high-flow-rate high-pressure steam in the flow-through heating step. The foam fusion is almost complete,
Here, it is only necessary to adjust the heating non-uniformity of the surface portion near the cavity wall of the molded body, and it is only necessary to finish the appearance of the molded body. In this process, it is no longer necessary to provide a large amount of high-pressure steam from both sides of the cavity as in the past by the flow-through heating process, and instead, the molding surface pressure is increased and the next cooling cycle time is lengthened. It is disadvantageous just to put it away.

【0021】以上の低圧蒸気による両面加熱方法によっ
て、発泡加熱の最終時点で更に膨張しようとしている発
泡体の面圧をできるだけ低くできて、冷却サイクルタイ
ムを短くできるだけでなく、加熱サイクルタイム自体も
従来の方法に比べて格段に短くすることができるのであ
る。
By the above two-sided heating method using low-pressure steam, the surface pressure of the foam to be expanded further at the final point of the foaming heating can be reduced as much as possible, and the cooling cycle time can be shortened. The method can be made much shorter than in the method described above.

【0022】このような両面加熱の終了後、冷却装置
(図示せず)を作動させて両金型1,2内に冷却水を散布
し、キャビティを構成する雄型1b,雌型2bの裏面を急速
に冷却し、然る後、真空装置により冷却を促進させる。
冷却が完了すれば型開きを行って発泡発泡成形体4aを取
り出す。
After completion of such double-sided heating, a cooling device
(Not shown) to spray cooling water into both the dies 1 and 2 to rapidly cool the back surfaces of the male mold 1b and the female mold 2b constituting the cavity, and then cool by a vacuum device Promote.
When the cooling is completed, the mold is opened to take out the foamed molded foam 4a.

【発明の効果】本発明方法では、通流加熱時に高圧大流
量の蒸気を使用してキャビティ内の成形体の内部融着を
完了させ、然る後、低圧蒸気による両面加熱を行うこと
で成形体の面圧を低くし、金型内での冷却時間を短くす
る事ができ、それ故発泡成形時間の短縮化を達成でき
た。
According to the method of the present invention, the internal fusion of the molded body in the cavity is completed by using high-pressure, large-flow steam during the flow heating, and then the double-sided heating is performed by the low-pressure steam. The surface pressure of the body can be reduced, and the cooling time in the mold can be shortened, so that the foaming molding time can be shortened.

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

【図1】本発明にかかる発泡成形機の通流加熱時の概略
断面図である。
FIG. 1 is a schematic sectional view of a foam molding machine according to the present invention at the time of flowing heat.

【符号の説明】[Explanation of symbols]

1…移動金型 1a…金型本体 1b…雄型 1d…移動側蒸気室 1e…蒸気噴出小孔 2…固定金型 2a…金型本体 2b…雌型 2d…固定側蒸気室 2e…蒸気噴出小孔 3…キャビティ 4…発泡予備発泡粒 5…蒸気出口(ドレン弁) 6…蒸気出口(ドレン弁) 1… Movable mold 1a… Mold body 1b… Male mold 1d… Movable steam chamber 1e… Steam jet small hole 2… Fixed mold 2a… Mold body 2b… Female mold 2d… Fixed steam chamber 2e… Steam jet Small holes 3 ... Cavities 4 ... Pre-expanded particles 5 ... Steam outlet (drain valve) 6 ... Steam outlet (drain valve)

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭60−116432(JP,A) 特開 昭63−21133(JP,A) 特開 平3−23929(JP,A) (58)調査した分野(Int.Cl.7,DB名) B29C 44/00 - 44/60 B29C 67/20 ──────────────────────────────────────────────────続 き Continuation of front page (56) References JP-A-60-116432 (JP, A) JP-A-63-21133 (JP, A) JP-A-3-23929 (JP, A) (58) Field (Int.Cl. 7 , DB name) B29C 44/00-44/60 B29C 67/20

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 型閉めされた移動金型と固定金型との間
に形成されたキャビティ内に発泡樹脂の予備発泡粒を充
填し、移動金型及び固定金型それぞれに高温蒸気を通し
て金型加熱を行い、金型加熱の完了後キャビティ内にお
いて予備発泡粒間を高温蒸気が高圧で通流するように0.
8〜1.0kg/cm2の蒸気圧にて一方の金型から他方の金型に
向かって高温蒸気を所定時間通流させて、前記予備発泡
粒を急速に発泡成形させる通流加熱を行い、然る後、両
金型の蒸気出口を閉じ、0.4〜0.5kg/cm2の蒸気圧にてキ
ャビティ内の発泡成形体の表面を焼き上げる両面加熱を
行う事を特徴とする発泡樹脂の発泡成形方法。
1. A pre-expanded foam of foamed resin is filled in a cavity formed between a closed moving mold and a fixed mold, and high-temperature steam is passed through each of the moving mold and the fixed mold. Heating is performed so that high-temperature steam flows at high pressure between the pre-expanded particles in the cavity after the completion of mold heating.
High-temperature steam is allowed to flow from one mold to the other mold at a vapor pressure of 8 to 1.0 kg / cm 2 for a predetermined time, and a flow heating for rapidly foaming and molding the pre-expanded particles is performed. After that, the steam outlets of both molds are closed, and a double-sided heating is performed to bake the surface of the foamed molded body in the cavity with a vapor pressure of 0.4 to 0.5 kg / cm 2. .
JP3299882A 1991-10-19 1991-10-19 Foam molding method for foamed resin Expired - Fee Related JP3055831B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3299882A JP3055831B2 (en) 1991-10-19 1991-10-19 Foam molding method for foamed resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3299882A JP3055831B2 (en) 1991-10-19 1991-10-19 Foam molding method for foamed resin

Publications (2)

Publication Number Publication Date
JPH05104649A JPH05104649A (en) 1993-04-27
JP3055831B2 true JP3055831B2 (en) 2000-06-26

Family

ID=17878090

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3299882A Expired - Fee Related JP3055831B2 (en) 1991-10-19 1991-10-19 Foam molding method for foamed resin

Country Status (1)

Country Link
JP (1) JP3055831B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH075716U (en) * 1993-06-29 1995-01-27 俊夫 広瀬 Back side mold
JP2013176886A (en) * 2012-02-28 2013-09-09 Sekisui Kaseihin Sakura:Kk In-mold foam molding method

Also Published As

Publication number Publication date
JPH05104649A (en) 1993-04-27

Similar Documents

Publication Publication Date Title
US4092385A (en) Method of producing molded parts with a smooth noncellular skin and a cellular core from foamable thermoplastic material
US4390486A (en) Method and apparatus for heating a mold cavity uniformly
WO2018040553A1 (en) Foam molding die for plastic structural member and molding method
JP3055831B2 (en) Foam molding method for foamed resin
JP3403016B2 (en) Method for producing synthetic resin molded article having hollow part
JPS588335B2 (en) Method and device for manufacturing foamed resin moldings
CN110978358A (en) Rotational molding preparation process of large plastic product
KR101030595B1 (en) injection mold apparatus
JPH05212810A (en) Die heat insulation structure of intra-die foam molding machine
JP2017132127A (en) Molding method of expanded resin product
JPS6153208B2 (en)
JPS581657B2 (en) Kanetsuhouhou
CN207206919U (en) A kind of foaming molding mold of plastic structural part
CN221819324U (en) A foam mold having easy foam forming
JP2621664B2 (en) Method for producing porous structure
JPS5922662B2 (en) Injection molding method and equipment
JPH0218979B2 (en)
JPS6315138B2 (en)
CN109551705B (en) Plastic integrated forming die
JP3814956B2 (en) Thermoplastic resin foam molding method
JPH09141715A (en) Injection mold apparatus
JPS62271729A (en) Manufacture of foamed resin molded product
JP2557681B2 (en) Manufacturing method of foamed resin molded product with skin
JPH0632344Y2 (en) Foam molding machine equipped with raw material filler
US20040142053A1 (en) Method and system for molding low density polymer articles

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080414

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090414

Year of fee payment: 9

LAPS Cancellation because of no payment of annual fees