JPS6121813B2 - - Google Patents

Info

Publication number
JPS6121813B2
JPS6121813B2 JP54040330A JP4033079A JPS6121813B2 JP S6121813 B2 JPS6121813 B2 JP S6121813B2 JP 54040330 A JP54040330 A JP 54040330A JP 4033079 A JP4033079 A JP 4033079A JP S6121813 B2 JPS6121813 B2 JP S6121813B2
Authority
JP
Japan
Prior art keywords
components
component
runner
mold
mixed
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
JP54040330A
Other languages
Japanese (ja)
Other versions
JPS55133936A (en
Inventor
Takao Nomura
Yoshio Taguchi
Kunio Naganami
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.)
Toyota Motor Corp
AGC Inc
Original Assignee
Asahi Glass Co Ltd
Toyota Motor Corp
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 Asahi Glass Co Ltd, Toyota Motor Corp filed Critical Asahi Glass Co Ltd
Priority to JP4033079A priority Critical patent/JPS55133936A/en
Publication of JPS55133936A publication Critical patent/JPS55133936A/en
Publication of JPS6121813B2 publication Critical patent/JPS6121813B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/0061Moulds or cores; Details thereof or accessories therefor characterised by the configuration of the material feeding channel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C67/00Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/24Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 characterised by the choice of material
    • B29C67/246Moulding high reactive monomers or prepolymers, e.g. by reaction injection moulding [RIM], liquid injection moulding [LIM]

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 本発明は反応射出成形法に関するものであり、
特にランナーに閉塞された分枝を設けてランナー
を流れる液状成分の最初の流れが成形型中に流れ
こむことを防止したランナーを使用した反応射出
成形法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a reaction injection molding method,
In particular, it relates to reaction injection molding processes using runners in which the runners are provided with closed branches to prevent the initial flow of liquid components flowing through the runners from flowing into the mold.

反応射出成形(Reaction Injection Molding)
は、ポリウレタンなどの混合により速やかに反応
を起す複数の液状成分から形成される合成樹脂の
成形に用いられる方法である。ポリウレタンの場
合、通常少くとも2個のイソシアネート基を有す
るイソシアネート化合物を主成分とする液状成分
と、少くとも2個の活性水素を有する活性水素化
合物、たとえばポリエーテルポリオールやポリエ
ステルポリオールを主成分とする液状成分との2
成分から形成される。反応射出成形は、これら複
数の液状成分を混合し射出する混合射出機と、成
形型とから主に構成される装置によつて行なわ
れ、混合射出機と成形型とを連結するランナーは
通常成形型と一体的にかつ成形型の分離面に設け
られている。これは成形型を開いて成形物を取り
出す際、ランナー内の硬化物も同時に取り出すこ
とが必要であるためである。
Reaction Injection Molding
is a method used for molding synthetic resins formed from a plurality of liquid components that quickly react when mixed together, such as polyurethane. In the case of polyurethane, it usually consists of a liquid component mainly consisting of an isocyanate compound having at least two isocyanate groups and an active hydrogen compound having at least two active hydrogens, such as a polyether polyol or a polyester polyol. 2 with liquid component
Formed from ingredients. Reaction injection molding is performed using a device that mainly consists of a mixing injection machine that mixes and injects these multiple liquid components and a mold, and the runner that connects the mixing injection machine and the mold is usually a molding machine. It is provided integrally with the mold and on the separation surface of the mold. This is because when opening the mold and taking out the molded product, it is necessary to take out the cured material inside the runner at the same time.

混合射出機は通常加圧された複数の液状成分を
衝突混合させて成形型へ送り出すものである。こ
のため、各液状成分の流れを開閉する機構と各液
状成分を衝突混合させる混合装置を有する。具体
的には、たとえば特開昭49−21465号報や特開昭
53−9854号公報に記載された装置がある。また、
ランナーの具体例としては、特開昭49−74758号
公報に記載されたものがある。このランナーには
後混合装置が設けられており、またこのランナー
には成形型の分離面と同一の分離面が設けられ、
ランナー内の硬化物はランナーを開いて取り出す
ことができるようになつている。
A mixing injection machine normally collides and mixes a plurality of pressurized liquid components and sends the mixture to a mold. For this reason, it has a mechanism for opening and closing the flow of each liquid component and a mixing device for collision-mixing each liquid component. Specifically, for example, JP-A-49-21465 and JP-A-Sho.
There is a device described in Japanese Patent No. 53-9854. Also,
A specific example of the runner is one described in Japanese Patent Application Laid-Open No. 49-74758. This runner is provided with a post-mixing device, and this runner is provided with a separation surface that is identical to the separation surface of the mold;
The cured material inside the runner can be taken out by opening the runner.

反応射出成形において、混合される複数の成分
は目的の割合で均一に混合されることが必要であ
る。複数の成分が目的の割合で均一に混合されな
いと、硬化反応やその進む時間が不均一になり成
形物の物性に悪影響を及ぼすばかりでなく、充填
不足や外観の不均一を生じ易くなる。混合割合の
不均一が最も起り易い部分は、複数の成分の射出
が開始される時である。複数の成分の射出は、そ
れぞれの射出口を開くことによつて行なわれる
が、この射出口を開く時間の調節がずれて複数の
成分の射出開始時が全く同一とならない場合と起
り易い。従つて射出開始時の複数の成分の混合物
の混合割合がそれ以後の混合割合をは異つてく
る。また、射出口を開く時間が全く同一であつた
としても、複数の成分の射出圧が異るために混合
割合が異つてくる場合もある。たとえば、1つの
成分の粘度が他の成分よりも高い場合、射出開始
時の射出圧がそれ以後の射出圧よりも低くなるこ
とがある。さらに、同時に射出されて混合された
混合物に別の射出口から射出された成分をさらに
混入する場合、その射出の時間的調節はさらに困
難となる。たとえば、2成分が混合室に射出され
て生じた混合物がランナーを流れて成形型に送ら
れる際にランナー部でこの混合物に第3の成分を
混入しようとすると、最初の2成分が射出されて
から第3の成分を混入する位置にくるまで第3の
成分の射出開始を遅らせなければならないからで
ある。この第3の成分の射出の時間的調節は極め
て困難であり、成形型に送られる混合物の最初の
部分は第3の成分が不足したり過剰となる場合が
起り易い。
In reaction injection molding, it is necessary that the plurality of components to be mixed be uniformly mixed in a desired ratio. If a plurality of components are not uniformly mixed in the desired proportions, the curing reaction and the time it takes to proceed will become uneven, which will not only adversely affect the physical properties of the molded product, but also likely cause insufficient filling and non-uniform appearance. The part where non-uniform mixing ratios are most likely to occur is when injection of multiple components is initiated. Injection of a plurality of components is performed by opening the respective injection ports, but it is likely that the opening times of the injection ports may be deviated and the injection start times of the plurality of components may not be exactly the same. Therefore, the mixing ratio of the mixture of a plurality of components at the start of injection differs from the subsequent mixing ratio. Further, even if the opening time of the injection port is exactly the same, the injection pressures of the plurality of components may be different, so that the mixing ratio may be different. For example, if one component has a higher viscosity than another component, the injection pressure at the start of injection may be lower than subsequent injection pressures. Furthermore, when a component injected from another injection port is further mixed into the mixture injected and mixed at the same time, it becomes even more difficult to adjust the timing of the injection. For example, when two components are injected into a mixing chamber and the resulting mixture flows through a runner and is sent to a mold, if an attempt is made to mix a third component into the mixture in the runner, the first two components will be injected. This is because the start of injection of the third component must be delayed until the third component is mixed in. Timing control of the injection of this third component is extremely difficult, and the initial portion of the mixture sent to the mold is likely to lack or have an excess of the third component.

本発明者は、反応射出成形において射出開始時
に複数の成分の混合割合が目的の混合割合と異つ
た部分が生じることを防ぐ方法を検討した。しか
し、複数の成分の射出開始の時間的調節は、混合
射出機の機械的電気的調節では困難であるばかり
でなく、複数の成分やその混合物の粘度等の物性
によつても時間的調節を変える必要があるなどの
理由により、その問題の解決は到底困難と考えら
れた。そこで、本発明者は複数の成分が射出され
て混合された混合物の流れの最初の部分(極端な
場合、1つの成分のみからなる場合も考えられ
る)を成形型に送らず、それ以後の混合物を成形
型に送ることによりこの問題の解決を図つた。こ
れにより、目的の混合割合の混合物のみを成形型
に送ることができ、上記時間的調節の問題の解決
は不要となる。そこで本発明者は、通常の少くと
も2成分を用いた反応射出成形に比較して時間的
調節の問題が大きい通常の少くとも2成分とさら
にそれら各成分より粘度の高い第3成分との少く
とも3成分の反応射出成形において、これら少く
とも3成分の混合物の最初の流れを成形型に送ら
ない方法を検討した。その結果、ランナー部に分
枝を設け、混合物の最初の流れが流れ込む分枝ラ
ンナーを閉塞された分枝ランナーとし、かつこの
分枝ランナー内で硬化した硬化物を取り出し可能
とするために成形型に通じる分枝ランナーと同様
閉塞された分枝ランナーにも離面を設けることを
見い出した。本発明はこの反応射出成形法に関す
るものであり、即ち、混合されることにより急速
に反応を起して合成樹脂を形成しうる複数の成分
を混合し成形型に射出して成形を行う反応射出成
形法において、複数の成分を混合することよりも
急速な反応を起す少なくとも2成分と該少なくと
も2成分のいずれよりも粘度の高い第3の成分と
からなる少なくとも3成分とすること、これら少
なくとも3成分の混合物を成形型の内部空間に送
るランナーに該混合物が最初に流れ込む閉塞され
た分岐ランナーを少なくとも1つ設けること、お
よび該閉塞された分岐ランナーに長さ方向の分離
面を設けて該ランナーを分割可能なランナーとす
ること特徴とする反応射出成形法である。
The present inventor studied a method for preventing the mixing ratio of a plurality of components from occurring at a portion where the mixing ratio differs from the intended mixing ratio at the start of injection in reaction injection molding. However, timing control of the injection start of multiple components is not only difficult with mechanical and electrical control of a mixing injection machine, but also due to physical properties such as viscosity of multiple components and their mixtures. The problem was thought to be extremely difficult to solve due to the need for change. Therefore, the inventor of the present invention did not send the first part of the mixture flow (in extreme cases, it may consist of only one component) of the mixture in which multiple components are injected and mixed, and instead We attempted to solve this problem by sending the material to the mold. As a result, only the mixture having the desired mixing ratio can be sent to the mold, and there is no need to solve the above-mentioned problem of time adjustment. Therefore, the inventor of the present invention has developed a method using conventional reaction injection molding that uses at least two components and a third component that has a higher viscosity than each of those components, which has a greater problem in time control than the conventional reaction injection molding that uses at least two components. In reaction injection molding of all three components, a method was investigated in which the initial flow of the mixture of at least three components was not sent to the mold. As a result, a branch is provided in the runner part, and the branch runner into which the first flow of the mixture flows is made into a closed branch runner, and the molding mold is made so that the cured material cured within this branch runner can be taken out. It was discovered that a closed branch runner, as well as a branch runner that leads to a block, has a separation surface. The present invention relates to this reaction injection molding method, that is, a reaction injection method in which a plurality of components that can rapidly react and form a synthetic resin when mixed are mixed and injected into a mold to perform molding. In the molding method, at least three components are formed, consisting of at least two components that react more rapidly than when a plurality of components are mixed, and a third component that has a higher viscosity than any of the at least two components; providing at least one closed branch runner into which the mixture initially flows into a runner for conveying the mixture of ingredients into the interior space of the mold; and providing the closed branch runner with a longitudinal separation surface to form the runner; This is a reaction injection molding method characterized by making a runner into a separable runner.

第1図および第2図に本発明の方法を用いた成
形型を、第3図ないし第6図に混合射出機の断面
図を示す。第1図は本発明におけるランナーを有
する成形型の下型の分離面を示す図である。第2
図は閉じた成形型の断面を示す図である。下型1
の分離面上にランナー2が設けられ、このランナ
ーの分岐点3以後は閉塞された分枝ランナー(4)と
成形型内部空間5に通じるランナー6に分けられ
ている。混合射出機7はピストン弁を有する混合
射出機であり、その詳細は第3図ないし第6図に
示されている。後記するように第1の成分は第1
の導入管8から、第2の成分は第2の導入管9か
ら、さらに第3の成分は2本の第3の導入管1
0,11から混合射出機7内の混合室12に導入
される。ただし、各成分が射出されていない時、
第1の成分は第1の排出管13から第2の成分は
第2の排出管14からそれぞれの容器に戻され循
環される。ただし、第3の成分は循環されない。
第2図は、上型15と下型1とを合せて閉じた成
形型の閉塞された分枝ランナー4を通る断面で切
断した図である。成形型の分離面を示す分離線1
6は成形型と1体的に設けられたランナーを通
り、ランナー全体を分割可能にしている。
FIGS. 1 and 2 show a mold using the method of the present invention, and FIGS. 3 to 6 show cross-sectional views of a mixing injection machine. FIG. 1 is a view showing the separation surface of the lower die of a mold having a runner in the present invention. Second
The figure shows a cross section of a closed mold. Lower mold 1
A runner 2 is provided on the separating surface of the runner, and the runner after the branch point 3 is divided into a closed branch runner (4) and a runner 6 communicating with the mold interior space 5. The mixing injection machine 7 is a mixing injection machine with a piston valve, the details of which are shown in FIGS. 3 to 6. As described later, the first component is the first component.
the second component from the second inlet pipe 9, and the third component from the two third inlet pipes 1.
0 and 11 into the mixing chamber 12 in the mixing injection machine 7. However, when each component is not injected,
The first component is returned to the respective containers through the first discharge pipe 13 and the second component is circulated through the second discharge pipe 14. However, the third component is not recycled.
FIG. 2 is a cross-section taken through the closed branch runner 4 of a mold in which the upper mold 15 and the lower mold 1 are closed together. Separation line 1 indicating the separation surface of the mold
6 passes through a runner provided integrally with the mold, making the entire runner separable.

第3図は混合射出機7の各成分が射出されてい
ない時の縦断面図、第4図は各成分が射出されて
いる時の縦断面図、第5図は第3図におけるa−
a′における横断面図、および第6図は同じくb−
b′における横断面図である。混合射出機7は弁ピ
ストン17とシリンダー18とから構成され、弁
ピストン17は第1の成分が流れる第1の溝19
と第2の成分が流れる第2の溝20を有してい
る。第3図の各成分が射出されていない時、第1
の成分は第1の導入管8から第1の溝19を通つ
て第1の排出管13から排出されて循環し、同様
に第2の成分は第2の導入管9、第2の溝20お
よび第2の排出管14を通つて循環する。第3の
成分は第5図および第6図に示すように循環され
ず、弁ピストン17によりその2つの導入管1
0,11が閉じられている。ピストン弁17が上
昇するとピストン弁17先端に混合室12が形成
され、3つの成分が各導入管から同時に混合室1
2に流れ込み混合される。図では第3の成分は2
つの導入管から導入されているが勿論1つの導入
管から導入されてもよい。しかし、第3の成分を
2つに分け互いに衝突する方向から導入する方が
混合性能が向上する。
FIG. 3 is a vertical cross-sectional view of the mixing injection machine 7 when each component is not injected, FIG. 4 is a vertical cross-sectional view when each component is injected, and FIG. 5 is a--a in FIG. 3.
The cross-sectional view at a′ and FIG.
FIG. The mixing injection machine 7 consists of a valve piston 17 and a cylinder 18, the valve piston 17 having a first groove 19 through which the first component flows.
and a second groove 20 through which the second component flows. When each component in Figure 3 is not injected, the first
The component is circulated from the first inlet pipe 8 through the first groove 19 and discharged from the first discharge pipe 13, and similarly, the second component is circulated through the second inlet pipe 9 and the second groove 20. and circulates through the second discharge pipe 14. The third component is not circulated as shown in FIGS.
0,11 are closed. When the piston valve 17 rises, a mixing chamber 12 is formed at the tip of the piston valve 17, and the three components are simultaneously introduced into the mixing chamber 1 from each introduction pipe.
2 and mixed. In the figure, the third component is 2
Although it is introduced through two introduction tubes, it may of course be introduced through one introduction tube. However, mixing performance is improved by dividing the third component into two parts and introducing them from the direction in which they collide with each other.

3つの成分の混合物は第1図に示すように、ラ
ンナー2に流入し、さらにまず閉塞されたランナ
ー4に流れ込む。この閉塞された分岐ランナー4
が混合物で満たされると、それ以後の混合物は成
形型内部空間5に通じるランナー6を通つて成形
型内部空間5に流れ込む。成形型内部空間5が混
合物で満たされると混合射出機7が第3図に示し
た状態に戻り混合射出が終了する。次いで混合物
は硬化し、最後に成形物が成形型から取り出され
る。成形型が開く時、成形型と一体に設けられた
ランナーも開き、ランナー内に硬化物も取り出さ
れる。閉塞されたランナー4内には不適当な混合
割合の混合物が硬化しているが、これも同時に取
り出される。
The three component mixture flows into runner 2 and then into runner 4, which is first closed, as shown in FIG. This blocked branch runner 4
Once filled with the mixture, the subsequent mixture flows into the mold interior space 5 through a runner 6 that opens into the mold interior space 5 . When the mold interior space 5 is filled with the mixture, the mixing injection machine 7 returns to the state shown in FIG. 3, and the mixing injection is completed. The mixture is then cured and finally the molding is removed from the mold. When the mold is opened, the runner provided integrally with the mold also opens, and the cured material is also taken out into the runner. A mixture having an inappropriate mixing ratio is hardened in the closed runner 4, but this is also taken out at the same time.

第7図および第8図に本発明の方法を用いた他
の例を示す。第7図は第1図と同様な下型の分離
面を示す図であり、第8図は成形型を閉じた時の
c−c′断面を示す図である。上型21と下型22
とからなる成形型の下型22に2つの弁ピストン
が設けられ、第1の弁ピストン23は第3図ない
し第6図に示したような循環構造を有する弁ピス
トンであり、第1の成分と第2の成分とを射出す
る。第2の弁ピストン24は第3の成分のみを射
出するための弁ピストンであり、循環構造を有し
ていない。この2つの弁ピストンは1つのピスト
ン25で同時に駆動され、図の各成分が射出され
ていない状態からピストン25が引かれると3つ
の成分が同時にランナー26に流れ込む。このラ
ンナー26は2つに分枝し、2つの分岐ランナー
27,28の先端は閉塞されたランナー29,3
0となつている。2つの分岐ランナー27,28
の途中に成形型内部空間に通じるランナー31へ
通じる複数の流路が設けられており、この流路を
通つた混合物は互いに衝突して再混合した後成形
型内部空間へ流れ込む。射出が終り混合物が硬化
し、成形型が開かれると各ランナー内の硬化物は
成形物とともに取り出すことができる。
Other examples using the method of the present invention are shown in FIGS. 7 and 8. FIG. 7 is a view showing the separation plane of the lower mold similar to FIG. 1, and FIG. 8 is a view showing the c-c' cross section when the mold is closed. Upper mold 21 and lower mold 22
Two valve pistons are provided in the lower die 22 of a mold consisting of a first component, and the first valve piston 23 is a valve piston having a circulation structure as shown in FIGS. 3 to 6. and the second component. The second valve piston 24 is a valve piston for injecting only the third component and does not have a circulation structure. These two valve pistons are simultaneously driven by one piston 25, and when the piston 25 is pulled from the state in which each component is not injected, the three components flow into the runner 26 at the same time. This runner 26 branches into two, and the tips of the two branch runners 27 and 28 are closed runners 29 and 3.
It is 0. Two branch runners 27, 28
A plurality of channels leading to the runner 31 that communicates with the mold interior space are provided in the middle of the mold, and the mixture passing through these channels collides with each other and is remixed before flowing into the mold interior space. When the injection is completed, the mixture is cured, and the mold is opened, the cured material in each runner can be taken out together with the molded product.

反応射出成形は混合されることにより急速な反
応を起して合成樹脂を形成する複数の成分から合
成樹脂成形物を成形する場合に用いられる。たと
えば、ポリウレタン、不飽和ポリエステル樹脂、
エポキシ樹脂、ポリアミドなどの成形に用いられ
るが、特にポリウレタンの成形に適している。た
とえば、ポリウレタンのエラストマー、フオー
ム、硬質樹脂などの成形に適している。ポリウレ
タンの場合、第1の成分はイソシアネート化合物
を主成分とする液状成分であり、第2の成分は活
性水素化合物を主成分とする液状成分である。通
常はこの2成分を用いて成形が行なわれるが、さ
らに成分が増加し、3以上の成分による成形もあ
る。一方、充填剤含有ポリウレタンなどの充填剤
含有合成樹脂を成形する場合、従来はこれら少く
とも2成分に充填剤を分散して成形を行つてい
た。しかしながら、充填剤を含む成分は高粘度と
なり、またこれら成分は循環されるために種々の
不都合な問題を引き起す。そこで、充填剤は第3
の成分として第1の成分と第2の成分とは別個に
射出した方が有利と考えられた。勿論、充填剤の
みでは流動しないので、流動可能とするために液
体などを加えて、高粘度のスラリー状の液体ある
いはゲル状などの流動化しうる固体として使用さ
れる。この充填剤に加えられる液体はイソシアネ
ート化合物あるいは活性水素化合物が適してお
り、特にポリオールなどの活性水素化合物が好ま
しい。第3の成分における充填剤の割合は30重量
%以上、特に50重量%以上が適当である。この第
3の成分は、第1の成分や第2の成分と異り循環
されない。従つて、循環に伴う不都合な問題、た
とえば高圧を要すること器壁内面が摩耗し易いこ
とが解決される。充填剤としてはガラス繊維ミル
ドフアイバー、ガラス繊維チヨツプドストラン
ド、マイカ、その他の繊維状や平板状の補強効果
のある充填剤が好ましい。また、炭酸カルシウ
ム、水酸化アルミニウム、硫酸バリウムその他の
粉末充填剤も使用できる。
Reaction injection molding is used to mold synthetic resin moldings from a plurality of components that, when mixed, cause a rapid reaction to form a synthetic resin. For example, polyurethane, unsaturated polyester resin,
It is used for molding epoxy resins, polyamides, etc., but is particularly suitable for molding polyurethane. For example, it is suitable for molding polyurethane elastomers, foams, hard resins, etc. In the case of polyurethane, the first component is a liquid component whose main component is an isocyanate compound, and the second component is a liquid component whose main component is an active hydrogen compound. Usually, these two components are used for molding, but the number of components is increased, and there is also molding using three or more components. On the other hand, when molding a filler-containing synthetic resin such as filler-containing polyurethane, conventionally the filler has been dispersed in at least two of these components. However, components containing fillers have a high viscosity, and these components are recycled, causing various disadvantages. Therefore, the filler is the third filler.
It was considered advantageous to inject the first and second components separately. Of course, the filler alone will not flow, so a liquid or the like is added to make it flowable, and it is used as a fluidizable solid such as a high viscosity slurry liquid or gel. The liquid added to the filler is suitably an isocyanate compound or an active hydrogen compound, with active hydrogen compounds such as polyols being particularly preferred. The proportion of filler in the third component is suitably at least 30% by weight, particularly at least 50% by weight. This third component, unlike the first and second components, is not recycled. Therefore, the disadvantageous problems associated with circulation, such as the high pressure required and the tendency to wear the inner surface of the container wall, are solved. As the filler, glass fiber milled fibers, chopped glass fiber strands, mica, and other fibrous or flat plate-like reinforcing fillers are preferred. Also, powder fillers such as calcium carbonate, aluminum hydroxide, barium sulfate, and others can be used.

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

第1図および第2図はそれぞれ本発明の方法の
一例を用いた成形型の平面図および断面図であ
る。第3図および第4図は混合射出機の縦断面図
であり、第5図および第6図は第3図におけるA
−A′,B−B′部の横断面図である。また第7図
および第8図はそれぞれ本発明の方法の他の例を
用いた成形型の平面図および断面図である。 1,15,21,22……成形型、2,26…
…ランナー、4,29,30……閉塞されたラン
ナー、7……混合射出機、17,23,24……
弁ピストン。
1 and 2 are a plan view and a sectional view, respectively, of a mold using an example of the method of the present invention. Figures 3 and 4 are longitudinal sectional views of the mixing injection machine, and Figures 5 and 6 are A in Figure 3.
-A', BB' section cross-sectional view. 7 and 8 are a plan view and a sectional view, respectively, of a mold using another example of the method of the present invention. 1, 15, 21, 22...Mold, 2, 26...
...Runner, 4,29,30...Closed runner, 7...Mixing injection machine, 17,23,24...
valve piston.

Claims (1)

【特許請求の範囲】 1 混合されることにより急速な反応を起して合
成樹脂を形成しうる複数の成分を混合し成形型に
射出して成形を行なう反応射出成形法において、
複数の成分を混合されることにより急速な反応を
起す少なくとも2成分と該少なくとも2成分のい
ずれよりも粘度の高い第3の成分とからなる少な
くとも3成分とすること、これら少なくとも3成
分の混合物を成形型の内部空間に送るランナーに
該混合物が最初に流れ込む閉塞された分岐ランナ
ーを少なくとも1つ設けること、および該閉塞さ
れた分岐ランナーに長さ方向の分離面を設けて該
ランナーを分割可能なランナーとすることを特徴
とする反応射出成形法。 2 複数の成分が混合されることにより急速な反
応を起す2成分と第3の成分からなり、該3成分
が同時に混合されることを特徴とする特許請求の
範囲1の方法。 3 複数の成分が混合されることにより急速な反
応を起す2成分の混合物に第3の成分を混入する
ことを特徴とする特許請求の範囲1の方法。 4 第3の成分が充填剤と液状成分からなる高粘
度液体あるいは流動化しうる固体からなることを
特徴とする特許請求の範囲1の方法。
[Claims] 1. In a reaction injection molding method in which a plurality of components that can cause a rapid reaction to form a synthetic resin when mixed are mixed and molded by injection into a mold,
At least three components consisting of at least two components that cause a rapid reaction when mixed with a plurality of components and a third component that has a higher viscosity than either of the at least two components, a mixture of these at least three components Providing at least one closed branch runner through which the mixture first flows into the runner feeding into the interior space of the mold, and providing the closed branch runner with a longitudinal separation surface so that the runner can be divided. A reaction injection molding method characterized by forming a runner. 2. The method according to claim 1, comprising two components and a third component that cause a rapid reaction when a plurality of components are mixed, and the three components are mixed simultaneously. 3. The method according to claim 1, characterized in that a third component is mixed into a mixture of two components that causes a rapid reaction when a plurality of components are mixed. 4. The method according to claim 1, wherein the third component is a highly viscous liquid consisting of a filler and a liquid component or a fluidizable solid.
JP4033079A 1979-04-05 1979-04-05 Method for reactive injection forming Granted JPS55133936A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4033079A JPS55133936A (en) 1979-04-05 1979-04-05 Method for reactive injection forming

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4033079A JPS55133936A (en) 1979-04-05 1979-04-05 Method for reactive injection forming

Publications (2)

Publication Number Publication Date
JPS55133936A JPS55133936A (en) 1980-10-18
JPS6121813B2 true JPS6121813B2 (en) 1986-05-29

Family

ID=12577597

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4033079A Granted JPS55133936A (en) 1979-04-05 1979-04-05 Method for reactive injection forming

Country Status (1)

Country Link
JP (1) JPS55133936A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4564491A (en) * 1982-03-01 1986-01-14 General Motors Corporation Preparing glass flake reinforced reaction injection molded polymers
JPH0337931Y2 (en) * 1986-04-30 1991-08-12
US4800058A (en) * 1987-08-24 1989-01-24 Arco Chemical Company Method for the preparation of rigid cast or transfer molded thermoset polyurethane modified polyisocyanurate compositions
CN105008104B (en) * 2013-03-14 2017-05-10 米其林集团总公司 Gate design with plunging nozzle and a waste reservoir for separating off ratio material
CN106738978A (en) * 2017-02-13 2017-05-31 长沙金镂机械科技有限公司 For the runner system of reaction injection molding mould

Also Published As

Publication number Publication date
JPS55133936A (en) 1980-10-18

Similar Documents

Publication Publication Date Title
US3799199A (en) Device for mixing two components
US4030637A (en) Apparatus for dosing and mixing fluid reactants
US3599290A (en) Injection molding machines
US6468464B1 (en) Method and apparatus for injection molding parts
US3499387A (en) Plastic injection machines
US3954926A (en) Method of molding a composite reinforced foamed product
US3733156A (en) Injection moulding machines
EP0684125A2 (en) Method of manufacturing moulded parts through two-components reactive-systems with high filler content
US4308226A (en) Particulate-containing foamed plastic
JPS62502253A (en) High pressure kneading head and reactive component injection valve
EP2054217A1 (en) Device and method for processing thermosetting plastics
US4257992A (en) Method and an apparatus for the production of articles which consist of filler-containing synthetic material, in particular of foam
JPS6121813B2 (en)
US3063813A (en) Apparatus for producing fluid mixtures
US4307062A (en) Particulate-containing foamed plastic
JPS6142610B2 (en)
US3908966A (en) Mixing apparatus
US6297342B1 (en) Method and mixing head for producing a reaction mixture from an isocyanate and a higher-viscous polyol formulation
GB2035111A (en) Improvements in reactive injection molding
CA1134576A (en) Process and device for filling cavities, particularly mold cavities, with a reactive, flowable mixture
US4252446A (en) Mixing head for reactive components
US4572820A (en) Process and apparatus for the production of a flowable reaction mixture
US3897939A (en) Liquid injection molding apparatus
CN102729394A (en) Method and device for injection molding of foamed plastics product
US5030408A (en) Method of producing molded resin article