JPH0193317A - Injection molding method - Google Patents
Injection molding methodInfo
- Publication number
- JPH0193317A JPH0193317A JP62249867A JP24986787A JPH0193317A JP H0193317 A JPH0193317 A JP H0193317A JP 62249867 A JP62249867 A JP 62249867A JP 24986787 A JP24986787 A JP 24986787A JP H0193317 A JPH0193317 A JP H0193317A
- Authority
- JP
- Japan
- Prior art keywords
- mold
- foaming
- molten resin
- temperature
- resin
- 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.)
- Granted
Links
Landscapes
- Laminated Bodies (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、発泡による射出成形方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method of injection molding using foaming.
従来の発泡成形用の射出成形機にあっては、例えば熱可
塑性プラスチック原料或いは熱硬化性の樹脂などの射出
成形材料をスクリュを備えた加熱シリンダで溶かして射
出する射出機構と、金型を高圧で締付ける型締め機構、
これらを自動的に動かす制御機構より成り、樹脂をホッ
パから加熱シリンダ内へ落下せしめるとともに、発泡剤
を別ホッパから加熱シリンダ内へ落下させ、可塑化した
樹脂に発泡剤を混練し、スクリュを前進させて金型内に
高圧で注入し、発泡させて成形品を得る方法、即ち、成
形材料に発泡剤、例えばウレタンフオームや発泡ポリエ
チレンなどを加え、スポンジ状のプラスチック成形品を
作る成形方法や、始めに表皮層になる成形材料を圧入し
、後から発泡剤入りの内部成形材料を圧入する所謂サン
ドインチ成形法等もあるが、共に下記のような欠点を有
している。Conventional injection molding machines for foam molding include an injection mechanism that melts and injects injection molding materials such as thermoplastic raw materials or thermosetting resins using a heating cylinder equipped with a screw, and a mold that is heated to high pressure. A mold clamping mechanism that tightens with
It consists of a control mechanism that automatically moves these, causing the resin to fall from a hopper into a heating cylinder, and the foaming agent to fall from a separate hopper into the heating cylinder, kneading the foaming agent into the plasticized resin, and moving the screw forward. A molding method in which a foaming agent such as urethane foam or foamed polyethylene is added to the molding material to create a sponge-like plastic molded product. There is also a so-called sandwich molding method, in which a molding material that will become the skin layer is first press-fitted, and then an internal molding material containing a foaming agent is press-fitted, but both have the following drawbacks.
(1)発泡時の空気圧力により、冷却される成形材料に
生じるひげの発生は防止されるが、表面層まで発泡して
いるので、外観が汚くなる。(1) The air pressure during foaming prevents the formation of whiskers in the molding material being cooled, but since the foaming extends to the surface layer, the appearance becomes dirty.
(2)全体に発泡しているので、空気断熱性があり、サ
イクルタイムが長くなる。(2) Since the entire product is foamed, it has air insulation properties and the cycle time becomes longer.
(3)充填時点(スクリュ内部)からすでに発泡してお
り、射出有効圧が低いので、薄肉部への充填性が悪く、
形状が制限される。(3) Foaming has already occurred at the time of filling (inside the screw), and the effective injection pressure is low, making it difficult to fill thin-walled areas.
Shape is limited.
〔発明が解決しようとする問題点]
本発明は上述した如き事情に鑑み、成形品の外観を奇麗
に仕上げるとともに、薄肉部や複雑形状品でも成形でき
、かつサイクルタイムを短縮することができる射出成形
方法を提供することにある。[Problems to be Solved by the Invention] In view of the above-mentioned circumstances, the present invention provides an injection method that can finish the appearance of molded products neatly, can mold even thin-walled parts and products with complex shapes, and can shorten cycle time. The object of the present invention is to provide a molding method.
上記問題点を解決するための本発明の射出成形方法は、
樹脂の可塑化中に加熱シリンダ内では発泡反応を生起す
ることなく溶融樹脂中に混在し、金型内に注入後金型内
の冷却速度の速い部分の溶融樹脂温度では発泡せず、冷
却速度の遅い部分の溶融樹脂温度で発泡するように、発
泡物質をコーティング剤により被覆して二重構造とし、
発泡反応を生起するための所要温度及び所要保持時間を
調製した発泡剤を溶融樹脂に混線分散させた状態で、前
記加熱シリンダを経て前記金型内に注入し、前記金型内
での溶融樹脂の冷却速度の差により発泡反応に差を付与
して成形することを特徴としている。The injection molding method of the present invention for solving the above problems includes:
During the plasticization of the resin, it is mixed in the molten resin without causing a foaming reaction in the heating cylinder, and after being injected into the mold, the molten resin does not foam at the temperature of the part of the mold where the cooling rate is high, and the cooling rate is low. The foam material is coated with a coating agent to form a double structure so that it foams at the temperature of the molten resin in the slow part of the process.
A foaming agent prepared at the required temperature and for a required holding time to cause a foaming reaction is mixed and dispersed in the molten resin, and is injected into the mold through the heating cylinder, and the molten resin is mixed in the mold. The feature is that molding is performed by giving different foaming reactions due to differences in cooling rates.
加熱シリンダ内のスクリュ内部では樹脂は溶けるが発泡
剤の反応温度には達してないため、発泡剤は溶融樹脂中
に混在する。そして、溶融樹脂の温度は加熱シリンダを
経て金型内に注入される過程でさらに上昇し、発泡剤の
反応温度を越えるが、金型内に注入される迄の時間は短
時間であるため、発泡剤が発泡するまでには至らない。Although the resin melts inside the screw in the heating cylinder, the reaction temperature of the blowing agent has not been reached, so the blowing agent is mixed in the molten resin. The temperature of the molten resin rises further during the process of being injected into the mold through the heating cylinder, exceeding the reaction temperature of the blowing agent, but since the time until it is injected into the mold is short, The foaming agent does not foam.
そして、加熱シリンダを経て金型内に注入された溶融樹
脂は冷却固化する工程において、金型表面に近い溶融樹
脂(成形品の外部の樹脂層)は急冷され、そのため金型
表面に近い溶融樹脂中に混在している発泡剤には発泡樹
脂が固化する。その結果、成形品表面つまり外観の奇麗
なしかも強度も低下しない成形品が得られる。一方、金
型内部にある溶融樹脂(成形品の内部の樹脂層)は徐冷
され温度が下かりに(い状態にあり、溶融樹脂内の発泡
剤には発泡するに足る時間、前記発泡剤の反応温度以上
に保持されることとなり、発泡剤が反応して発泡する。In the process of cooling and solidifying the molten resin injected into the mold through the heating cylinder, the molten resin near the mold surface (the resin layer outside the molded product) is rapidly cooled, and therefore the molten resin near the mold surface The foamed resin solidifies in the foaming agent mixed therein. As a result, a molded product can be obtained that has a clean surface, that is, a molded product appearance, and has no decrease in strength. On the other hand, the molten resin inside the mold (resin layer inside the molded product) is slowly cooled and the temperature is lowered (in a low state), and the foaming agent in the molten resin has enough time to foam. The temperature will be maintained above the reaction temperature, and the foaming agent will react and foam.
この発泡時の発泡圧力によって金型内の溶融樹脂は内部
から膨張させられる。この膨張により樹脂の冷却時の収
縮による「ひけ」の発生を防止することが可能となる。The molten resin in the mold is expanded from the inside by the foaming pressure during this foaming. This expansion makes it possible to prevent the occurrence of "sink marks" caused by contraction of the resin when it is cooled.
以下、図面により本発明の一実施例としての射出成形方
法について説明すると、第1〜3図に示すように、本発
明を実施するのに好適な射出成形機は、スクリュ1を備
えた射出用の加熱シリンダ2、ノズル3、固定盤4、固
定金型5、可動金型6、スプル7、ヒータ8、ランナ9
、ゲート10、キャビティ11等の既知の各要素から成
形機本体が構成されている。Hereinafter, an injection molding method as an embodiment of the present invention will be explained with reference to the drawings. As shown in FIGS. 1 to 3, an injection molding machine suitable for carrying out the present invention is equipped with Heating cylinder 2, nozzle 3, fixed plate 4, fixed mold 5, movable mold 6, sprue 7, heater 8, runner 9
, a gate 10, a cavity 11, and other known elements constitute a molding machine main body.
そして、前記成形機本体部分に、加熱シリンダ2に風を
送って同シリンダ2内の剪断発熱量を吸収する冷却用ブ
ロアー風路12と、成形材料としての樹脂13及び発泡
剤14供給用のホッパ15とから成る構成が付設されて
いる。The molding machine main body includes a cooling blower air passage 12 for blowing air into the heating cylinder 2 and absorbing the shear heat generated in the cylinder 2, and a hopper for supplying resin 13 and foaming agent 14 as molding materials. A configuration consisting of 15 is attached.
また、前記発泡剤14としては、加熱シリンダ2内での
可塑中には樹脂13は溶けるが、発泡剤14は発泡反応
しないような樹脂13の融点より高い沸点を有する発泡
剤14を用いることにより、また、キャビティ11内の
溶融樹脂の冷却速度の差により、つまり冷却速度の速い
部分の樹脂温度(急冷された溶融樹脂の温度)では発泡
することがなく、冷却速度の遅い部分の樹脂温度(徐冷
された溶樹脂の温度)で発泡するように、発泡反応を生
起するための所要温度及び所要保持時間を調製した発泡
剤14を用いる。Further, as the foaming agent 14, the resin 13 melts during plasticization in the heating cylinder 2, but the foaming agent 14 has a boiling point higher than the melting point of the resin 13, which does not cause a foaming reaction. Furthermore, due to the difference in the cooling rate of the molten resin in the cavity 11, foaming does not occur at the resin temperature in the part where the cooling rate is fast (temperature of the rapidly cooled molten resin), and the resin temperature in the part where the cooling rate is slow ( The foaming agent 14 is adjusted to the required temperature and required holding time to cause the foaming reaction so that the foaming agent 14 foams at the temperature of the slowly cooled molten resin.
ぞして、具体的には、例えば、第2図に示すように、熱
をある時間、ある温度以上加えると、つまりある特定温
度(冷却速度の遅い部位の樹脂温度)以上で特定時間加
熱されると溶融し、成形材料と同じ材料であるが、分子
量を多くし、成形材料より融点を必要温度上げたプラス
チック材からなるコーティング剤16で発泡物質17を
被覆して顆粒状に固めた発泡剤14(例えばアゾジカル
ボン酸アミド或いは重曹)を用いる。Specifically, for example, as shown in Figure 2, when heat is applied for a certain period of time and above a certain temperature, that is, the resin is heated at a certain temperature (temperature of the resin in the area where the cooling rate is slow) or above for a certain period of time. The foamed substance 17 is coated with a coating agent 16 made of a plastic material, which is the same material as the molding material but has a higher molecular weight and a melting point higher than that of the molding material, and is solidified into granules. 14 (for example, azodicarboxylic acid amide or sodium bicarbonate).
次に本実施例における射出成形の操作について説明する
。まず固定金型5と可動金型6とを型締めした後、ホッ
パ15から樹脂13とコーティングされた発泡剤14を
送り、加熱シリンダ2内でスクリュ1の回転により混線
分散し、ノズル3より溶融樹脂を射出し、溶融樹脂にコ
ーティングされた発泡剤14を混入させるようにしたも
のである。Next, the injection molding operation in this example will be explained. First, after clamping the fixed mold 5 and the movable mold 6, the resin 13 and the coated foaming agent 14 are sent from the hopper 15, cross-dispersed by the rotation of the screw 1 in the heating cylinder 2, and melted from the nozzle 3. The resin is injected and the foaming agent 14 coated with the molten resin is mixed in.
つまり、本実施例では、溶融樹脂の射出と発泡剤の供給
を同軸上で行ない、この同軸上(スプル7)を流れる溶
融樹脂にコーティングされた発泡剤14を垂直方向から
直接混入している。That is, in this embodiment, the injection of the molten resin and the supply of the blowing agent are carried out on the same axis, and the coated blowing agent 14 is directly mixed into the molten resin flowing on the same axis (the sprue 7) from the vertical direction.
そして、コーティングされた発泡剤14が混入された溶
融樹脂はキャビティ11内に圧入され、以後従来の一般
的方法に従って、キャビティ11内のコーティングされ
た発泡剤14の混入された溶融樹脂を冷却固化した後、
離型する。The molten resin mixed with the coated blowing agent 14 was then press-fitted into the cavity 11, and the molten resin mixed with the coated blowing agent 14 in the cavity 11 was then cooled and solidified according to a conventional general method. rear,
Release the mold.
次に、第3図に加熱シリンダー内と金型内の温度変化を
示す。Next, FIG. 3 shows temperature changes inside the heating cylinder and inside the mold.
尚、第3図中の符号Jはコーテイング材の融点を示し、
Kは成形材料の融点を示し、Lは発泡剤の沸点を示して
いる。In addition, the symbol J in FIG. 3 indicates the melting point of the coating material,
K indicates the melting point of the molding material, and L indicates the boiling point of the blowing agent.
また第3図中の符号■はスクリュ1内部の温度変化領域
を示し、符号■はノズル3通過時の温度変化領域を示し
、符号■はスプル7通過時の温度変化領域を示し、符号
■はランチ9通過時の温度変化領域を示し、符号Vはゲ
ート10通過時の温度変化領域を示し、符号■は成形品
充填中及び収縮過程での温度変化領域を示している。Further, the symbol ■ in FIG. 3 indicates the temperature change area inside the screw 1, the symbol ■ indicates the temperature change area when passing the nozzle 3, the symbol ■ indicates the temperature change area when the sprue 7 passes, and the symbol ■ indicates the temperature change area when passing the nozzle 3. The temperature change area when passing through the launch 9 is shown, the code V shows the temperature change area when passing through the gate 10, and the code ■ shows the temperature change area during the filling of the molded product and the shrinking process.
さらに、実線■は金型表皮に近い成形材料の温度変化を
示し、破線■はコーテイング材内部の発泡する限界点で
の温度変化を示し、−点鎖線■は成′形品内部の成形材
料の温度変化を示している。Furthermore, the solid line ■ shows the temperature change of the molding material near the mold skin, the broken line ■ shows the temperature change at the foaming limit point inside the coating material, and the -dot-dashed line ■ shows the temperature change of the molding material inside the molded product. Shows temperature change.
前記冷却固化の工程において、加熱シリンダ2内のスク
リュ1内部では、成形材料としての樹脂13の融点がK
であることから樹脂13は溶けるが、コーティング剤1
6、発泡物質17はブロアー風路3に風を送って剪断発
熱量を吸収されているため、領域Iの如く反応温度には
達していない。金型内に溶融樹脂と発泡剤との混練され
たものを射出することにより、ノズル3を通過すると領
域■の如く温度が上がり、スプルヤ通過時の温度変化は
領域■となり、ランナ9通過時の温度変化は領域■とな
り、ゲート10通過時の温度変化は領域Vとなり、さら
に金型内の製品部への充填及び製品部充填後の温度変化
は領域■となる。In the cooling and solidifying step, the melting point of the resin 13 as the molding material is K.
Therefore, resin 13 melts, but coating agent 1
6. Since the foamed material 17 absorbs the shear heat generated by blowing air through the blower air path 3, it does not reach the reaction temperature as in region I. By injecting the kneaded mixture of molten resin and foaming agent into the mold, when it passes through the nozzle 3, the temperature rises as shown in the area ■, and the temperature change when passing through the sprayer is in the area ■, and when it passes through the runner 9, the temperature rises as shown in the area ■. The temperature change is in the region (2), the temperature change when passing through the gate 10 is in the region V, and the temperature change in the product section in the mold and after the product section is filled is in the region (2).
即ち、金型に近い部分では実線■の如き温度変化し、ひ
げの原因となる金型内の製品内部の徐冷部では一点鎖線
■の如き温度変化することになり、また、発泡剤14の
コーティング剤16が溶けて反応する熱仕事量の限界線
として破線■の如き温度変化をすることになり、従って
、破線4以上の一点鎖線■では発泡反応を生じ、一方、
破線■以下の実線■では発泡反応を生じないことになる
。つまり、発泡の沸点3以上での熱仕事量は、金型表皮
近くでは面積APBとなり発泡せず、一方向部では面積
APCとなり発泡することになる。That is, the temperature changes as shown by the solid line (■) in the area close to the mold, and the temperature changes as shown in the dashed line (■) in the annealing section inside the product inside the mold, which causes whiskers. As the limit line of thermal work when the coating agent 16 melts and reacts, the temperature changes as indicated by the broken line (■).Therefore, a foaming reaction occurs at the dashed line (2) above the dashed line (4), and on the other hand,
In the solid line ■ below the broken line ■, no foaming reaction occurs. In other words, the amount of thermal work at the foaming boiling point of 3 or higher is the area APB near the mold skin, which does not result in foaming, and the area APC in one direction, which results in foaming.
このように、金型内の製品部への充填中または直後まで
は非発泡状態で成形できるため、薄肉部や凸部の複雑形
状品を成形でき、しかも外観の奇麗な成形品を得ること
ができる。In this way, it is possible to mold in a non-foamed state during or immediately after filling the product part in the mold, so it is possible to mold products with complex shapes with thin walls and convex parts, and also to obtain molded products with a beautiful appearance. can.
また、ゲートシール後に樹脂の徐冷部が急冷部を引張っ
てひげが発生するのを防ぐ手段として、ゲート10を広
くしたり、射出圧力を上げていることから、ひげが少な
くなり、パリ、ソリも少なくなる。In addition, as a means to prevent the slow cooling part of the resin from pulling on the rapidly cooling part after gate sealing, the gate 10 is made wider and the injection pressure is increased, which reduces the number of cracks and warps. will also decrease.
さらに、局部のみの発泡のため、通常発泡よりサイクル
タイムが大幅に短縮することができる。Furthermore, since foaming is performed only locally, the cycle time can be significantly shortened compared to normal foaming.
尚、本実施例では成形材13とコーティングされた発泡
剤14とがそれぞれ別々にホッパ15内に入れられるこ
とになるが、発泡剤14が成形材13に混入されるよう
にしてもよい。In this embodiment, the molding material 13 and the coated foaming agent 14 are placed separately in the hopper 15, but the foaming agent 14 may be mixed into the molding material 13.
また、発泡物質17をコーティングせずに、単独で使用
してもよい。Further, the foamed material 17 may be used alone without being coated.
〔発明の効果]
以上、詳述したように本発明の射出成形方法は、金型内
の製品部への充填中または直後までは非発泡状態で成形
できることから、薄肉部や凸部の複雑形状品を形成でき
かつ外観の奇麗な成形品を得ることができるほか、局部
のみの発泡のため、通常発泡よりサイクルタイムを大幅
に短縮することができるという利点がある。[Effects of the Invention] As described in detail above, the injection molding method of the present invention can mold in a non-foamed state during or immediately after filling the product part in the mold, so it is possible to mold the product in a non-foamed state. In addition to being able to form a molded product with a beautiful appearance, this method also has the advantage that the cycle time can be significantly shortened compared to normal foaming because it foams only locally.
第1図は本発明の一実施例としての射出成形方法を実施
するに好適な射出成形機を示す概要断面図、第2図は発
泡剤を示す断面図、第3図は加熱シリンダ内と金型内の
温度変化を示す関係図である。
1・・・スクリュ、2・・・加熱シリンダ、3・・・ノ
ズル、4・・・固定盤、5・・・固定金型、6・・・可
動金型、7・・・スプル、8・・・ヒータ、9・・・ラ
ンナ、10・・・ゲート、11・・・キャビティ、12
・・・ブロアー風路、13・・・樹脂、14・・・発泡
剤、15・・・ホッパ、16・・・コーティング剤、1
7・・・発泡物質、■・・・スクリュ内部の温度変化領
域、■・・・ノズル通過時の温度変化領域、■・・・ス
プル通過時の温度変化領域、■・・・ランナ通過時の温
度変化領域、■・・・ゲート通過時の温度変化領域、■
・・・成形品充填中及び収縮過程での温度変化領域、■
・・・金型表皮に近い成形材料の温度変化、■・・・コ
ーテイング材内部の発泡する限界点での温度変化、■・
・・成形品内部の成形材料の温度変化、J・・・コーテ
イング材の融点、K・・・成形材料の融点、L・・・発
泡剤の沸点。
手続補正書
昭和63年9月7日Fig. 1 is a schematic sectional view showing an injection molding machine suitable for carrying out an injection molding method as an embodiment of the present invention, Fig. 2 is a sectional view showing a blowing agent, and Fig. 3 is a schematic sectional view showing the inside of the heating cylinder and the injection molding machine. FIG. 3 is a relationship diagram showing temperature changes within the mold. DESCRIPTION OF SYMBOLS 1... Screw, 2... Heating cylinder, 3... Nozzle, 4... Fixed plate, 5... Fixed mold, 6... Movable mold, 7... Sprue, 8... ...Heater, 9...Runner, 10...Gate, 11...Cavity, 12
... Blower air passage, 13 ... Resin, 14 ... Foaming agent, 15 ... Hopper, 16 ... Coating agent, 1
7... Foamed material, ■... Temperature change area inside the screw, ■... Temperature change area when passing through the nozzle, ■... Temperature change area when passing through the sprue, ■... Temperature change area when passing through the runner. Temperature change area, ■...Temperature change area when passing through the gate, ■
...Temperature change area during molded product filling and shrinkage process,■
...Temperature change in the molding material near the mold skin, ■...Temperature change at the foaming limit inside the coating material, ■.
...Temperature change of the molding material inside the molded product, J...Melting point of the coating material, K...Melting point of the molding material, L...Boiling point of the blowing agent. Procedural amendment September 7, 1986
Claims (1)
ることなく溶融樹脂中に混在し、金型内に注入後金型内
の冷却速度の速い部分の溶融樹脂温度では発泡せず、冷
却速度の遅い部分の溶融樹脂温度で発泡するように、発
泡物質をコーティング剤により被覆して二重構造とし、
発泡反応を生起するための所要温度及び所要保持時間を
調製した発泡剤を溶融樹脂に混線分散させた状態で、前
記加熱シリンダを経て前記金型内に注入し、前記金型内
での溶融樹脂の冷却速度の差により発泡反応に差を付与
して成形することを特徴とする射出成形方法。During the plasticization of the resin, it is mixed in the molten resin without causing a foaming reaction in the heating cylinder, and after being injected into the mold, the molten resin does not foam at the temperature of the part of the mold where the cooling rate is high, and the cooling rate is low. The foam material is coated with a coating agent to form a double structure so that it foams at the temperature of the molten resin in the slow part of the process.
A foaming agent prepared at the required temperature and for a required holding time to cause a foaming reaction is mixed and dispersed in the molten resin, and is injected into the mold through the heating cylinder, and the molten resin is mixed in the mold. An injection molding method characterized in that molding is performed by imparting a difference in foaming reaction due to a difference in cooling rate.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62249867A JPH0733030B2 (en) | 1987-10-05 | 1987-10-05 | Injection molding method |
| US07/360,933 US5049327A (en) | 1987-07-21 | 1988-07-20 | Injection molding method |
| KR1019890700487A KR950012850B1 (en) | 1987-07-21 | 1988-07-20 | Injection molding method |
| EP19880906104 EP0341310A4 (en) | 1987-07-21 | 1988-07-20 | Injection molding method |
| PCT/JP1988/000719 WO1989000489A1 (en) | 1987-07-21 | 1988-07-20 | Injection molding method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62249867A JPH0733030B2 (en) | 1987-10-05 | 1987-10-05 | Injection molding method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0193317A true JPH0193317A (en) | 1989-04-12 |
| JPH0733030B2 JPH0733030B2 (en) | 1995-04-12 |
Family
ID=17199369
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62249867A Expired - Lifetime JPH0733030B2 (en) | 1987-07-21 | 1987-10-05 | Injection molding method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0733030B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016160416A (en) * | 2015-03-05 | 2016-09-05 | 日立金属株式会社 | Pellet, foamed resin molding, foam insulated wire and cable |
| CN107250282A (en) * | 2015-02-05 | 2017-10-13 | 日本化药株式会社 | A thermosetting resin composition containing a polyol compound, an acid anhydride compound, and a thermosetting resin, a polycarboxylic acid resin, a thermosetting resin composition using the same, and any of the aforementioned thermosetting resin compositions Optical semiconductor device used as packaging material or reflective material |
-
1987
- 1987-10-05 JP JP62249867A patent/JPH0733030B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107250282A (en) * | 2015-02-05 | 2017-10-13 | 日本化药株式会社 | A thermosetting resin composition containing a polyol compound, an acid anhydride compound, and a thermosetting resin, a polycarboxylic acid resin, a thermosetting resin composition using the same, and any of the aforementioned thermosetting resin compositions Optical semiconductor device used as packaging material or reflective material |
| JP2016160416A (en) * | 2015-03-05 | 2016-09-05 | 日立金属株式会社 | Pellet, foamed resin molding, foam insulated wire and cable |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0733030B2 (en) | 1995-04-12 |
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