JPS58134720A - Preparation of formed product of foaming resin - Google Patents
Preparation of formed product of foaming resinInfo
- Publication number
- JPS58134720A JPS58134720A JP57017868A JP1786882A JPS58134720A JP S58134720 A JPS58134720 A JP S58134720A JP 57017868 A JP57017868 A JP 57017868A JP 1786882 A JP1786882 A JP 1786882A JP S58134720 A JPS58134720 A JP S58134720A
- Authority
- JP
- Japan
- Prior art keywords
- mold
- resin
- cavity
- temperature
- layer
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/02—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
- B29C44/04—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles consisting of at least two parts of chemically or physically different materials, e.g. having different densities
- B29C44/0407—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles consisting of at least two parts of chemically or physically different materials, e.g. having different densities by regulating the temperature of the mould or parts thereof, e.g. cold mould walls inhibiting foaming of an outer layer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
Landscapes
- Injection Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、片面に発泡層を有し他の面にスキン層を有す
る発泡樹脂成形品および表面全体かスキン層で包囲され
内部に発泡層を有する発泡樹脂成形品の製造方法に関す
るものである。Detailed Description of the Invention The present invention relates to a foamed resin molded product having a foam layer on one side and a skin layer on the other surface, and a foamed resin molded product whose entire surface is surrounded by a skin layer and has a foam layer inside. This relates to a manufacturing method.
従来、射出成形機において、発泡剤入りの溶融した熱可
塑性樹脂を金型内に高速で射出充填し、金型内の型面に
接した部分を冷却硬化させてスキン層を形成した後、金
型を一定の幅だけ開くことにより、内部の樹脂を発泡さ
せて表面全体がスキン層で包囲された発泡樹脂成形品を
得るという方法が公知である。この方法によれば、金型
の開くストローク(幅)によって発泡率を所定の大きさ
に決めることができ、高発泡率の成形品を比較的容易に
得ることができる。しかしながら、この従来の方法では
、射出時に樹脂が発熱し、その樹脂が発泡剤の分解開始
温度より高・温となって金型内に射出充填されるため、
金型内iで型面に接した部分が冷却硬化されて表面にス
キン層が形成される前に発泡が開始され、こめため、′
成形品の表面にガス跡(スワールマーク)が現出し、表
面の良好な成形品が得られない欠点があった。Conventionally, in an injection molding machine, a molten thermoplastic resin containing a blowing agent is injected into a mold at high speed, and the part of the mold in contact with the mold surface is cooled and hardened to form a skin layer. A known method is to open a mold by a certain width to foam the resin inside to obtain a foamed resin molded product whose entire surface is surrounded by a skin layer. According to this method, the foaming rate can be determined to a predetermined size depending on the opening stroke (width) of the mold, and a molded product with a high foaming rate can be obtained relatively easily. However, in this conventional method, the resin generates heat during injection, and the resin is injected and filled into the mold at a temperature higher than the decomposition starting temperature of the foaming agent.
Foaming starts before the part in contact with the mold surface inside the mold is cooled and hardened and a skin layer is formed on the surface,
There was a drawback that gas marks (swirl marks) appeared on the surface of the molded product, making it impossible to obtain a molded product with a good surface.
本発明は、表面にガス跡を発生させずに、平滑度の高い
スキン層を形成し得て良好な発泡樹脂成形品を得ること
のできる製造方法を提供するもの“ である。The present invention provides a manufacturing method capable of forming a highly smooth skin layer without generating gas traces on the surface and obtaining a good foamed resin molded product.
ところで、この種の発泡樹脂成形品の製造方法において
、表面が平滑でガス跡が生じないようにするには、
■ 射出完了までガスを発生させない、■ 射出時、成
形品の表皮形成時にガスを発生させない、
の
■ 射出時、樹脂からガスの飛散を防ぐ、■ 一旦生じ
た凹凸、ガス跡を金型内で修正して平滑にする、
■ 成形後、表面を平滑にする、
等の方法が烹見られる。By the way, in the manufacturing method of this type of foamed resin molded product, in order to ensure that the surface is smooth and that no gas traces occur, it is necessary to: ■ not generate gas until the injection is completed; and ■ do not generate gas during injection and when forming the skin of the molded product. There are several ways to prevent this from occurring, such as ■ Preventing gas from scattering from the resin during injection, ■ Correcting and smoothing any unevenness or gas traces that have occurred within the mold, ■ Smoothing the surface after molding. You can see the heat.
本発明方法ぽ、上記■の方法を基本とし、射出充填後に
樹脂thi′i□1玲面を加熱してこの片面から発泡さ
せ、他の面に長キン層を形成してガス跡のない平滑面を
有する良好な発泡樹脂成形品が得られるようにしたもの
である。The method of the present invention is based on method (2) above, and after injection and filling, one side of the resin thi'i□ is heated to foam from one side, and a long layer is formed on the other side to create a smooth surface without gas traces. This makes it possible to obtain a good foamed resin molded product having a surface.
すなわち、本発明の第1の方法は、発泡剤を添加した樹
脂を射出装置により樹脂の溶融温度より高くかつ発泡剤
の分解開始湿度より低い温度で可塑化混練して金型キャ
ピテイ内に射出充填した後、金型キャビティの相対向す
る2つの型面のうち一方の型面を発泡剤の分解開始温度
以上に加熱し、キャビティ内の樹脂をこの加熱された型
面側から発泡させつつ、金型を発泡量に相当するストロ
ーク分だけ開くことにより、キャピテイ内において、加
熱された型面側に樹脂の発泡層を、他の型面に接する樹
脂の表面にスキン層を成形し、然る後、金型を冷却して
キャピテイ内の成形品を冷却し、金型を全開して該成形
品を取出すようにしたことを特徴とするものである。That is, the first method of the present invention is to plasticize and knead a resin to which a blowing agent has been added using an injection device at a temperature higher than the melting temperature of the resin and lower than the decomposition start humidity of the blowing agent, and then inject and fill the resin into a mold cavity. After that, one of the two opposing mold surfaces of the mold cavity is heated to a temperature higher than the decomposition temperature of the foaming agent, and the resin in the cavity is foamed from this heated mold surface side, and the metal is heated. By opening the mold by a stroke corresponding to the foaming amount, a foam layer of resin is formed on the heated mold surface side and a skin layer is formed on the surface of the resin that is in contact with the other mold surface in the cavity. This is characterized in that the mold is cooled to cool the molded product in the cavity, and the mold is fully opened to take out the molded product.
また、本発明の第2の方法は、上記第1の方法によりキ
ャビティ内で樹脂の発泡層とスキン層を成形した後、金
型を一旦冷却してキャビティ内あ樹脂を一旦冷却した後
、前記発泡層を形成させた型面を再度加熱し、この型面
に接する発泡層の表面を溶融させてスキン層を成形する
ことにより、表面がスキン層で包囲され内部に発泡層を
有する発泡樹脂成形品を成形し、然る後、金型を再度冷
却して該成形品を冷却し、金型を全開して該成形品を取
出すようにしたことを特徴とするものである。Further, in the second method of the present invention, after molding the resin foam layer and skin layer in the cavity by the first method, the mold is once cooled to once cool the resin in the cavity, and then the resin foam layer and skin layer are molded in the cavity. By heating the mold surface on which the foam layer has been formed again and melting the surface of the foam layer in contact with this mold surface to form a skin layer, the surface is surrounded by the skin layer and the foam layer is inside the foam resin molding. This method is characterized in that a product is molded, and then the mold is cooled again to cool the molded product, and the mold is fully opened to take out the molded product.
以下、本発明を図に示す実施例に基づいて説明する。Hereinafter, the present invention will be explained based on embodiments shown in the drawings.
1は従来公知の射出装置、2は該射出装置1の前面に設
けた固定盤、3は該固定盤2に□相対向して複数本のタ
イロッド(図示省略)により軸線方向に摺動自在に設け
た可動盤、4および5は固定盤2と可動盤3のそれぞれ
の相対向する面に固定して設けたUいに軸線方向に着脱
自在に嵌合する一対の金型、6は両金型4.5によって
形成されるキャビティを示す。1 is a conventionally known injection device, 2 is a stationary plate provided on the front side of the injection device 1, and 3 is opposite to the stationary plate 2 and is slidable in the axial direction by a plurality of tie rods (not shown). The provided movable plates 4 and 5 are a pair of molds that are removably fitted in the axial direction of the U-shaped molds fixed to the opposite surfaces of the fixed plate 2 and the movable plate 3, respectively, and 6 is a pair of molds that are removably fitted in the axial direction. The cavity formed by mold 4.5 is shown.
固定側の金型4は、キャビティ6の型面6a。The mold 4 on the fixed side is a mold surface 6a of the cavity 6.
6bを形成する。可動側の金型5は、取付板5aにコア
5bを固着し、かつ、型板5Cをコア5bに嵌合させて
ガイドピンとはね(図示せず)により取付板5aに軸線
方向摺動自在に支持させてなり、キャビティ乙の型面6
c e ’ 6dを形成する。Form 6b. The mold 5 on the movable side has a core 5b fixed to the mounting plate 5a, and a mold plate 5C is fitted to the core 5b, so that it can freely slide in the axial direction on the mounting plate 5a by means of guide pins and springs (not shown). The mold surface 6 of cavity B is supported by
Form ce' 6d.
なお、可動側金型5は、図外の型締装置とストローク調
節装置により、型板5cが固定側金型4に密着しかつコ
ア5bの先端がキャビティ6内に進入した型締位置と、
型締位置から型板5Cが固定側金型4に密着したままで
後述する発泡剤の発泡量に見合ったストローク8分だけ
コア5bが後退した調節位置たとえばコア先端の型面6
dが型板5Cの内側の型面60き同一面となる位置き、
コア5bおよび型板5Cが固定側金型4から脱出および
開離した金型開放位置とに位置変更自在とする。前記ス
トローク調節装置には、たとえば特公昭52−2542
9号公報または特公昭54−11827号公報に開示さ
れた装置等を用いる。The movable mold 5 is set to a clamping position where the mold plate 5c is in close contact with the fixed mold 4 and the tip of the core 5b has entered the cavity 6 by a mold clamping device and a stroke adjustment device (not shown);
An adjustment position where the core 5b is retreated by a stroke of 8 minutes commensurate with the foaming amount of the foaming agent, which will be described later, while the mold plate 5C remains in close contact with the stationary mold 4 from the mold clamping position, for example, the mold surface 6 at the tip of the core.
The position where d is the same surface as the mold surface 60 inside the mold plate 5C,
The core 5b and the mold plate 5C are able to escape from the stationary mold 4 and change their positions to a mold open position where they are separated. For example, the stroke adjusting device is disclosed in Japanese Patent Publication No. 52-2542.
The apparatus disclosed in Japanese Patent No. 9 or Japanese Patent Publication No. 54-11827 is used.
コア5bは銅等の熱伝導率の高い材料にて形成し、その
内部において型面6dに近い部分に熱媒−1
流体用通路7を設ける。臀へ板5aには該通路に連通ず
る熱媒流体の流入ロアa、および流出ロアbを設ける。The core 5b is made of a material with high thermal conductivity such as copper, and a heat medium-1 fluid passage 7 is provided inside the core 5b in a portion close to the mold surface 6d. The buttock plate 5a is provided with an inflow lower a and an outflow lower b for the heating medium fluid, which communicate with the passage.
熱媒流体には一般に油を用い、前記流入ロアaおよび7
bには、油圧ポンプ8、切換弁9、加熱器10、冷却器
11、逆止弁11,12等を備えた油圧回路を接続し、
油圧ポンプ8の吐出油を切換弁9の切換えにより加熱器
10または冷却器11に供給して加熱または冷却した後
、逆止弁11または12を経て前記流入ロアaに供給し
、前記通路7を通過させ、流出ロアbからタンク15に
戻すことによって、コア5bを加熱または冷却できるよ
うに構成する。14はリリーフ弁である。なお、熱媒流
体の温度は、金型構造により異なるが、加熱時には発泡
剤の分解最適温度T2より30〜60℃程度高く、冷却
時には5〜10℃程度となるように、前記加熱器10お
よび冷却器11の性能を考慮する。Oil is generally used as the heat transfer fluid, and the inflow lowers a and 7
A hydraulic circuit including a hydraulic pump 8, a switching valve 9, a heater 10, a cooler 11, check valves 11 and 12, etc. is connected to b.
After the oil discharged from the hydraulic pump 8 is supplied to the heater 10 or the cooler 11 to be heated or cooled by switching the switching valve 9, the oil is supplied to the inflow lower a through the check valve 11 or 12, and the passage 7 is The core 5b is configured to be heated or cooled by allowing the core 5b to pass through and returning to the tank 15 from the outflow lower b. 14 is a relief valve. Although the temperature of the heat transfer fluid varies depending on the mold structure, the heater 10 and The performance of the cooler 11 will be considered.
次に、上記の如く構成した装置により、発泡樹脂成形品
を製造する場合について説明する。Next, a case will be described in which a foamed resin molded product is manufactured using the apparatus configured as described above.
まず、第1図に示す如く、金型を周知の型締装置’、I
f ””’lj
置により型締L1可動側金型5のコア5bの先端をキャ
ビティ6内に進入させた型締位置に保持した状態で、発
泡剤を添加した熱可塑性樹脂を射出装置1により可塑化
混練してキャビティ6内に射出充填する。ただし、この
樹脂の可塑化混練および射出充填時には、樹脂の温度を
、樹脂の溶融温度Tmより高温とするが、従来のように
発泡剤の分解開始温度T1より高くするのではなく、該
分解開始温度Tlより低温となるように制御する。この
制御は射出速度等の成形条件や射出装置1のノズル径を
大径にする等によって行う。また、この射出充填時には
、ポンプ8を停止し、コア5bの通路7に対する熱媒流
体の供給を停止しておく。なお、3位置切換弁を用い、
該切換弁の中立位置でポンプの吐出油をタンクに戻し、
コア側への熱媒流体の供給回路をブロックするようにし
てもよい。First, as shown in FIG.
f ””'lj While the tip of the core 5b of the movable mold 5 of the mold clamp L1 is held in the mold clamping position where it enters the cavity 6, a thermoplastic resin to which a foaming agent has been added is injected by the injection device 1. The mixture is plasticized and kneaded and then injected and filled into the cavity 6. However, during plasticization, kneading, and injection filling of this resin, the temperature of the resin is set higher than the melting temperature Tm of the resin, but the temperature is not set higher than the decomposition start temperature T1 of the blowing agent as in the conventional method, but when the decomposition starts. The temperature is controlled to be lower than the temperature Tl. This control is performed by changing molding conditions such as injection speed and increasing the nozzle diameter of the injection device 1. Further, during this injection filling, the pump 8 is stopped and the supply of heat medium fluid to the passage 7 of the core 5b is stopped. In addition, using a 3-position switching valve,
At the neutral position of the switching valve, the pump discharge oil is returned to the tank,
The supply circuit of the heat medium fluid to the core side may be blocked.
このように、発泡剤を添加した樹脂を、該樹脂の溶融温
度Tmより高温で、発泡剤の分解開始温度Tlより低温
で可塑化混練してキャビティ6内に射出充填することに
より、樹脂が発泡せずにキャビティ6内に充填される。In this way, the resin is foamed by plasticizing and kneading the resin to which a foaming agent has been added at a temperature higher than the melting temperature Tm of the resin and lower than the decomposition start temperature Tl of the foaming agent and injected into the cavity 6. The inside of the cavity 6 is filled without any process.
然る後、ポンプ8を駆動し、切換弁9を図面右位置に切
換え、熱媒流体としての油を加熱器10、逆止弁12を
経て流入ロアaに流入させ、コア5b内の通路7を通過
させてタンク15に仄すことによって、通路7に高温油
を供給し、コア5bを発泡剤の分解最適温度72以上に
加熱する。なお、固定側金型4は従来と同様に強制加熱
せずに常湿のままとしておく。これにより、キャビティ
6内の樹脂が、固定側金型4の型面6a、6bおよび型
板5Cの型面6Cに接した部分は発泡せずに、加熱され
たコア5bの型面6dに接した部分から発泡し始める。After that, the pump 8 is driven, the switching valve 9 is switched to the right position in the drawing, and the oil as a heat transfer fluid flows into the inflow lower a through the heater 10 and the check valve 12, and the passage 7 in the core 5b is caused to flow into the inlet lower a. By passing through the tank 15, high-temperature oil is supplied to the passage 7, and the core 5b is heated to a temperature equal to or higher than the optimum temperature 72 for decomposing the blowing agent. Note that the stationary mold 4 is kept at normal humidity without being forcibly heated as in the conventional case. As a result, the resin in the cavity 6 contacts the mold surface 6d of the heated core 5b without foaming at the portions in contact with the mold surfaces 6a, 6b of the stationary mold 4 and the mold surface 6C of the mold plate 5C. It will start foaming from the exposed area.
次いで、上記樹脂の発泡を行いながら、可動側金型5を
樹脂の発泡量に見合ったストローク8分だけ後退させる
。この可動側金型5の後退は、公知のストローク調節装
置により可動盤6と一体に後退させることによって行う
。そして、第2図に示すように、コア5bの型面6dが
型fM5cのを面6cと同一面になる位置まで金型を開
いて−は停止させ、この状態で上記樹脂を充分に発泡さ
せる。Next, while foaming the resin, the movable mold 5 is moved back by a stroke of 8 minutes commensurate with the foaming amount of the resin. The movable mold 5 is moved back together with the movable platen 6 using a known stroke adjustment device. Then, as shown in FIG. 2, the mold is opened to a position where the mold surface 6d of the core 5b is flush with the surface 6c of the mold fM5c, and the mold is stopped. In this state, the resin is sufficiently foamed. .
次いで、切換弁9を図示の位置に戻すことにより、前記
ポンプ8の吐出油を冷却器11.逆比弁12を経て流入
ロアaに流入させ、コア5b内の通路7を通過させてタ
ンク15に戻し、これによってフ了5bを冷却する。こ
のとき、固定側金型4に対し、周知の手段で冷却水等を
供給し、冷却する。こうして金型4,5を冷却すること
によりキャビティ6内の樹脂を冷却し、然る後、可動側
金型5を周知の手段により後退させて金型4,5を全開
し、キャビティ6内の樹脂すなわち成形品を取出す。Next, by returning the switching valve 9 to the illustrated position, the oil discharged from the pump 8 is transferred to the cooler 11. It flows into the inflow lower a through the inverse ratio valve 12, passes through the passage 7 in the core 5b, and returns to the tank 15, thereby cooling the fluid 5b. At this time, cooling water or the like is supplied to the stationary mold 4 by a known means to cool it. By cooling the molds 4 and 5 in this way, the resin in the cavity 6 is cooled, and then the movable mold 5 is moved back by well-known means to fully open the molds 4 and 5. Remove the resin, that is, the molded product.
こうして成形した成形品は、第6図に示すように、キャ
ビティ6内において固定側金型4の型面6a、6bおよ
び型板5cの型面6cに接していた表面側にスキン層A
が形成され、コア5bの型面6dに接していた表面側に
発泡層Bが形成され、ぐ
たものとなる。この成形品によりば、スキン層Aの表面
AIおよび側面(周面)A2が、その成形時に1′)・
前記型面6a、6b、6cによっ゛て終始低温に保持さ
れているので、未発泡のままでガス跡のない平滑な表面
に形成され、発泡層Bの表面にのみガス跡が表われるこ
とになる。従って、発泡層Bを裏側にして用いることに
より、カバー等に有効に使用できる。As shown in FIG. 6, the molded product thus formed has a skin layer A on the surface side that was in contact with the mold surfaces 6a, 6b of the stationary mold 4 and the mold surface 6c of the mold plate 5c in the cavity 6.
is formed, and a foam layer B is formed on the surface side of the core 5b that was in contact with the mold surface 6d, resulting in a gummy product. According to this molded product, the surface AI and the side surface (peripheral surface) A2 of the skin layer A are kept at a low temperature from beginning to end by the mold surfaces 6a, 6b, and 6c during the molding process. A smooth surface with no gas traces is formed as it is foamed, and gas traces appear only on the surface of the foam layer B. Therefore, by using the foam layer B on the back side, it can be effectively used for covers, etc.
ところで、上記工程において、キャビティ6内で樹脂を
発泡させ、金型を冷却してキャビティ6内の樹脂を一旦
冷却した後、その成形品(このときは第3図に示す構造
となっている)を取出す前に、コア5bを前述した方法
で再度加熱し、型面6dに接する樹脂(発泡層)の表面
を溶融させ、然る後、再度金型を冷却し、キャビティ6
内の樹脂(成形品)を冷却して取出せば、第4図に示す
ような成形品が得られる。この成形品によれば、基本的
には第5図に示す成形品と同一構造であるが、前記型面
6dによる再加熱により発泡層Bの表面がソリッド状と
なってこの表面にもスキン層A′が形成され、以って、
内部のみに発泡層Bを有し11
し、表面全体がスキン層A 、 A’にて包囲されたも
胃i1・:1゜
のとなり、第6図に示す成形品に比べてその用途を拡大
できることになる。By the way, in the above process, after the resin is foamed in the cavity 6, the mold is cooled, and the resin in the cavity 6 is once cooled, the molded product (at this time, the structure is shown in FIG. 3) is formed. Before taking out the core 5b, the core 5b is heated again using the method described above to melt the surface of the resin (foamed layer) in contact with the mold surface 6d, and then the mold is cooled again to form the cavity 6.
If the resin (molded product) inside is cooled and taken out, a molded product as shown in FIG. 4 will be obtained. This molded product basically has the same structure as the molded product shown in FIG. 5, but the surface of the foam layer B becomes solid due to reheating by the mold surface 6d, and a skin layer is also formed on this surface. A′ is formed, so
It has a foam layer B only on the inside, and the entire surface is surrounded by skin layers A and A', resulting in a stomach i1:1°, which expands its uses compared to the molded product shown in Figure 6. It will be possible.
実施例1
樹脂材料としてポリエチレン樹脂を用い、’1剤として
り、P、Tのアミルジコート剤を使用した。この樹脂の
溶融温fil Tmは160℃であり、発泡剤の特性(
分解性能)は第5図a、bに示す通りである。第5[i
Jaは温度と時間の関係を示す。Example 1 Polyethylene resin was used as the resin material, and P and T amyl dicoating agents were used as the '1 agent. The melting temperature fil Tm of this resin is 160°C, and the characteristics of the blowing agent (
The decomposition performance) is as shown in FIGS. 5a and 5b. Fifth [i
Ja indicates the relationship between temperature and time.
温度上昇は5°C/分である。同図aにおいて、この発
泡剤の分解開始温度TIは175℃、分解最適温度T2
は220°Cであることがわかる。第5図すは時間とガ
ス量の関係を示す。The temperature rise is 5°C/min. In Figure a, the decomposition initiation temperature TI of this foaming agent is 175°C, and the optimum decomposition temperature T2
It can be seen that the temperature is 220°C. Figure 5 shows the relationship between time and gas amount.
上記材料を用いて、本発明方法により発泡樹脂成形品を
製造した。このときの樹脂温度は第6図に示す知〈制御
した。第6図において、線Iは射出装置1内の樹脂の温
度、illは金型キャビティ6内に射出充填された樹脂
の型面6a側の温度、線画は同樹脂の型面6d側の温度
、線層′は再加熱されるときの型面6d側の樹脂の温度
を示す。A foamed resin molded article was manufactured using the above material and the method of the present invention. The resin temperature at this time was controlled as shown in FIG. In FIG. 6, line I is the temperature of the resin in the injection device 1, ill is the temperature of the resin injected and filled into the mold cavity 6 on the mold surface 6a side, and line drawing is the temperature of the same resin on the mold surface 6d side. The line layer' indicates the temperature of the resin on the mold surface 6d side when it is reheated.
すなわち、第6図で明らかなように、第1の方法におい
て、発泡剤を混入した樹脂を、射出装置1により発泡剤
の分解開始温度’l+(175℃)より低温で可塑化混
練し、次いで、該分解開始温度T1より低温でかつ樹脂
の溶融温度Tm (160℃)以上の温度で金型キャビ
ティ6内に射出充填し、キャビティ6の固定側金型4の
型面6a側の温度を線画に示すように前記分解開始温度
TI以下とLながら、コア5bの型面6d側の湿度を線
画に示すように発泡剤の分解最適湿度220℃近く(2
10°C)まで加熱しつつ、金型を所定のストローク分
だけ開き、然る後、金型を冷却して樹脂を冷却し、金型
を全開してその成形品を取出し、第6図に示す発泡樹脂
成形品を製造した。これにより、スキン層Aの表面AI
および側面A2のいずれにも全くガス跡がなく、表面が
平滑な発泡樹脂成形品が得られた。That is, as is clear from FIG. 6, in the first method, the resin mixed with the blowing agent is plasticized and kneaded using the injection device 1 at a temperature lower than the decomposition start temperature 'l+ (175° C.) of the blowing agent, and then , the mold cavity 6 is injected and filled at a temperature lower than the decomposition start temperature T1 and higher than the melting temperature Tm (160° C.) of the resin, and the temperature on the mold surface 6a side of the fixed mold 4 of the cavity 6 is plotted as a line drawing. As shown in the line drawing, the humidity on the mold surface 6d side of the core 5b is close to 220°C (220°C), which is the optimum humidity for decomposition of the foaming agent, while the decomposition start temperature TI is below TI.
10°C), open the mold by a predetermined stroke, then cool the mold to cool the resin, fully open the mold and take out the molded product, as shown in Figure 6. The following foamed resin molded product was manufactured. As a result, the surface AI of skin layer A
A foamed resin molded product with a smooth surface and no gas traces on either side A2 was obtained.
実施例2
上記実施例1と同じ樹脂材料および発泡剤を用い、かつ
、実施例1と同じ方法でスキン層と発泡層を形成した後
、その成形品を金型から取出す前に、第6図の線画′に
示すようにコア5bを再加熱し、発泡層の表面を溶融さ
せてスキン層A′を形成した後、金型を冷却して成形品
を冷却し、金型を全開して成形品を取出し、第4図に示
す発泡樹脂成形品を製造した。これにより内部にのみ発
泡層Bを有し、全表面がスキン層A 、 A’により包
囲され、かつ、全表面にガス跡がなく、平滑な表面を呈
する発泡樹脂成形品が得られた。Example 2 After forming a skin layer and a foam layer in the same manner as in Example 1 using the same resin material and foaming agent as in Example 1 above, and before taking out the molded product from the mold, as shown in FIG. After reheating the core 5b and melting the surface of the foam layer to form the skin layer A' as shown in the line drawing ', the mold is cooled to cool the molded product, and the mold is fully opened to mold. The product was taken out, and a foamed resin molded product shown in FIG. 4 was manufactured. As a result, a foamed resin molded product was obtained which had the foamed layer B only inside, the entire surface was surrounded by the skin layers A and A', and had no gas traces on the entire surface and had a smooth surface.
上記実施例1および2において、樹脂の金型キャ゛ビテ
ィへの射出充填時に、高速射出を行った場合、樹脂の温
度が発泡剤の分解開始温度T1以上さらには分解最適温
度12以上になることもあるが、第5図すで明らかなよ
うに、瞬時の発熱であれば分解最適温度12以上−とな
っても差支えない。In Examples 1 and 2 above, if high-speed injection is performed when injecting and filling the resin into the mold cavity, the temperature of the resin will exceed the blowing agent's decomposition start temperature T1 or higher, and furthermore, the optimum decomposition temperature 12 or higher. However, as is clear from FIG. 5, if the heat generation is instantaneous, there is no problem even if the optimum decomposition temperature is 12 or higher.
以上の如く、本発明によれば、片面に発泡層を有し、他
の面にスキン層を有する発泡樹脂成形品を容易に製造で
きる。しかも、スキン層にはガス跡が生じることなく、
平滑な表面に成形でき、良好な成形品が得られる。と七
に、金型の温度制御のみでガス跡の問題を解決讐き、か
つ、スキン層の厚みならびに発泡層の厚みを自由に制御
できる。As described above, according to the present invention, a foamed resin molded product having a foam layer on one side and a skin layer on the other side can be easily manufactured. Moreover, there is no gas trace on the skin layer,
It can be molded onto a smooth surface, resulting in a good molded product. Seventh, the problem of gas traces can be solved by controlling the temperature of the mold, and the thickness of the skin layer and the foam layer can be freely controlled.
また、機械的には、射出装置にノズルバルブヲ使用しな
くてもよく、金型のみの改良で表面の良好な発泡樹脂成
形品が得られるのである。In addition, mechanically, there is no need to use a nozzle valve in the injection device, and a foamed resin molded product with a good surface can be obtained by improving only the mold.
さらに、本発明の第2の方法によれば、内部にのみ発泡
層を有し、表面全体がガス跡のない平滑面のスキン層を
有する発泡樹脂成形品を得ることができ、その汎用性を
高め、商品価値の高い成形品が得られる。しかも、この
成形時には、上記第1の方法と同じ金型を用い、第1の
方法と連続した工程で実施でき、量産性の向上にも寄与
できる。Furthermore, according to the second method of the present invention, it is possible to obtain a foamed resin molded product having a foamed layer only inside and a skin layer with a smooth surface without gas traces on the entire surface, which increases its versatility. molded products with high commercial value. Furthermore, this molding can be performed using the same mold as in the first method and in a continuous step with the first method, which can also contribute to improving mass productivity.
第1図は本発明方法の実施に用いられる金型の一例を示
す断面図、第2図はその金型を発泡量に対応するストロ
ーク分だけ開いた状態の要部断面図、第3図は本発明の
第1の方法により成形した発泡樹脂成形品の断面図、第
4図は同第2の方法により成形し尼′発泡樹脂成形品の
断面図、第5図a、bは発泡−の分解性能を示す図、第
6図は本発明方法によ不樹脂湿度の制御の一例を示す図
である。 1・
1・・・射出装置、2・・・固定盤、3・・・可動盤、
4・・・固定側金型、5・・・可動側金型、5a・・・
取付板、5b・・・コア、5C・・・型板、6・・・キ
ャピテイ、7熱媒流体通路、8・・ポンプ、9・・・切
換弁、10・・・加熱器、11・・・冷却器、12.1
3・・・逆比弁。
特許出願人 株式会社神戸製鋼所
−・ニレ・
第 1 図
第 2 図
第 3 図
第 41り(
第 5 図
第 6121Fig. 1 is a cross-sectional view showing an example of a mold used to carry out the method of the present invention, Fig. 2 is a cross-sectional view of the main part of the mold in a state where the mold is opened by a stroke corresponding to the amount of foaming, and Fig. 3 is a cross-sectional view of the main part of the mold. FIG. 4 is a cross-sectional view of a foamed resin molded product molded by the first method of the present invention, FIG. 5 is a cross-sectional view of a foamed resin molded product molded by the second method, and FIGS. FIG. 6, which is a diagram showing the decomposition performance, is a diagram showing an example of controlling the non-resin humidity by the method of the present invention. 1. 1... Injection device, 2... Fixed plate, 3... Movable plate,
4... Fixed side mold, 5... Movable side mold, 5a...
Mounting plate, 5b... Core, 5C... Template plate, 6... Capity, 7 Heat medium fluid passage, 8... Pump, 9... Switching valve, 10... Heater, 11...・Cooler, 12.1
3...Reverse ratio valve. Patent Applicant Kobe Steel, Ltd. - Elm Figure 1 Figure 2 Figure 3 Figure 41 (Figure 5 Figure 6121)
Claims (1)
融温度より高くかつ発泡剤の分解開始温度より低い温度
で可塑化混練して金型キャビティ内に射出充填した後、
金型キャピテイの相対向する2つの型面のうち一方の型
面を発泡剤の分解開始温度以上に加熱し、キャビティ内
の樹脂をこの加熱された型面側から発泡させつつ、金型
を発泡量に相当するストローク分だけ開くことにより、
キャビティ内において、加熱された型面側に樹脂の発泡
層を、他の型面に接する樹脂の表面にスキン層を成形し
、然る後、金型を冷却してキャビティ内の成形品を冷却
し、金型を全開して該成形品を取出すようにしたと七を
特徴とする発泡樹脂成形品の製造方法。 2、 発泡剤を添加した樹脂を射出装置により樹脂の溶
融温度より高くかつ発泡剤の分解開始温度より低い温度
で可塑化混練して金型キャビティ内に射出充填した後、
金型キャビティの相対向する2つの型面のうち一方の型
面を発泡剤の分解開始温度以上に加熱し、キャビティ内
の樹脂をこの加熱された型面側から発泡させつつ、金型
を発泡層に相当するストローク分だけ開くことにより、
キャビティ内において、加熱された型面側に樹脂の発泡
層を、他の型面に接する樹脂の表面にスキン層を成形し
、次いで、金型を冷却してキャビティ内の樹脂を一旦冷
却した後、前記発泡層を形成させた型面を再度加熱し、
この型面に接する発泡層の表面を溶融させてスキン層を
成形することにより、表面がスキン層で包囲され内部に
発泡層を有する発泡樹脂成形品を成形し、然る後、金型
を再度冷却して該成形品を冷却し、金型を全開して該成
形品を取出すようにしたことを特徴にする発泡樹脂成形
品の製造方法。[Claims] 1. After plasticizing and kneading the resin to which a blowing agent has been added using an injection device at a temperature higher than the melting temperature of the resin and lower than the decomposition start temperature of the blowing agent, and injecting and filling the resin into a mold cavity,
One of the two opposing mold surfaces of the mold cavity is heated above the decomposition temperature of the foaming agent, and the resin in the cavity is foamed from this heated mold surface side, causing the mold to foam. By opening the stroke corresponding to the amount,
Inside the cavity, a foamed resin layer is molded on the heated mold surface side, and a skin layer is molded on the resin surface that is in contact with the other mold surface, and then the mold is cooled to cool the molded product inside the cavity. 7. A method for manufacturing a foamed resin molded product, characterized in that the mold is fully opened to take out the molded product. 2. After plasticizing and kneading the resin to which the foaming agent has been added using an injection device at a temperature higher than the melting temperature of the resin and lower than the decomposition start temperature of the foaming agent, the resin is injected and filled into the mold cavity.
One of the two opposing mold surfaces of the mold cavity is heated above the decomposition temperature of the foaming agent, and the resin in the cavity is foamed from this heated mold surface side, causing the mold to foam. By opening the stroke corresponding to the layer,
Inside the cavity, a foamed resin layer is molded on the heated mold surface side, and a skin layer is molded on the resin surface that is in contact with the other mold surface.Then, the mold is cooled and the resin in the cavity is cooled once. , heating the mold surface on which the foam layer was formed again;
By melting the surface of the foam layer in contact with the mold surface and molding a skin layer, a foamed resin molded product whose surface is surrounded by the skin layer and has a foam layer inside is molded, and then the mold is replaced again. A method for manufacturing a foamed resin molded article, characterized in that the molded article is cooled and the mold is fully opened to take out the molded article.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57017868A JPS58134720A (en) | 1982-02-05 | 1982-02-05 | Preparation of formed product of foaming resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57017868A JPS58134720A (en) | 1982-02-05 | 1982-02-05 | Preparation of formed product of foaming resin |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58134720A true JPS58134720A (en) | 1983-08-11 |
Family
ID=11955643
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57017868A Pending JPS58134720A (en) | 1982-02-05 | 1982-02-05 | Preparation of formed product of foaming resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58134720A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1989000489A1 (en) * | 1987-07-21 | 1989-01-26 | Sumitomo Heavy Industries, Ltd. | Injection molding method |
-
1982
- 1982-02-05 JP JP57017868A patent/JPS58134720A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1989000489A1 (en) * | 1987-07-21 | 1989-01-26 | Sumitomo Heavy Industries, Ltd. | Injection molding method |
US5049327A (en) * | 1987-07-21 | 1991-09-17 | Sumitomo Heavy Industries, Ltd. | Injection molding method |
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