JP5532288B2 - Release agent supply device - Google Patents

Release agent supply device Download PDF

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JP5532288B2
JP5532288B2 JP2009044746A JP2009044746A JP5532288B2 JP 5532288 B2 JP5532288 B2 JP 5532288B2 JP 2009044746 A JP2009044746 A JP 2009044746A JP 2009044746 A JP2009044746 A JP 2009044746A JP 5532288 B2 JP5532288 B2 JP 5532288B2
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release agent
dispersion chamber
cavity
valve
air supply
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JP2010194600A (en
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基治 近藤
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Aisin Corp
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Aisin Seiki Co Ltd
Aisin Corp
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Description

本発明は成形用モールドのキャビティに粉体状の離型剤を塗布する離型剤供給装置に関する。   The present invention relates to a release agent supply apparatus for applying a powder release agent to a cavity of a molding mold.

この種の離型剤供給装置に関連する先行技術文献情報として下記に示す特許文献1がある。この特許文献1に記された離型剤供給装置は、離型剤を収納する離型剤タンクと、キャビティと離型剤タンクとの間に設けられ、キャビティと連通した縦型の中継室と、離型剤タンクから一定量の離型剤を抽出して中継室に供給する抽出装置と、中継室内に一定量の離型剤が供給された時点で離型剤をキャビティに空気で圧送する圧送機構とを備えている。したがって、抽出装置によって略正確に抽出された離型剤をキャビティに圧送することができる。   There exists patent document 1 shown below as prior art document information relevant to this kind of mold release agent supply apparatus. The release agent supply device described in Patent Document 1 includes a release agent tank that stores a release agent, a vertical relay chamber that is provided between the cavity and the release agent tank, and communicates with the cavity. An extraction device that extracts a predetermined amount of release agent from the release agent tank and supplies it to the relay chamber, and when the predetermined amount of release agent is supplied into the relay chamber, the release agent is pumped by air into the cavity And a pressure feeding mechanism. Therefore, the mold release agent extracted almost accurately by the extraction device can be pumped into the cavity.

さらに、この種の離型剤供給装置に関連する他の先行技術文献情報として下記に示す特許文献2がある。この特許文献2に記された離型剤供給装置では、中継室(供給管)とキャビティとの間に、中継室とキャビティとを接続する配管よりも大きな内径の拡散部が設けられている。そのため、離型剤は、拡散部に流入するときの径の急増に伴う拡散により、拡散部で分散されるので均一な付着が行われるという趣旨の効果が記されている。   Furthermore, there is Patent Document 2 shown below as other prior art document information related to this type of release agent supply apparatus. In the release agent supply apparatus described in Patent Document 2, a diffusion portion having an inner diameter larger than that of the pipe connecting the relay chamber and the cavity is provided between the relay chamber (supply pipe) and the cavity. For this reason, the release agent is dispersed in the diffusion portion due to diffusion accompanying a rapid increase in the diameter when flowing into the diffusion portion, so that the effect that uniform adhesion is performed is described.

特開2003−275855号公報(0029段落、図4)Japanese Patent Laying-Open No. 2003-275855 (paragraph 0029, FIG. 4) 特開2004−223562号公報(0022段落、図5)JP 2004-223562 A (paragraph 0022, FIG. 5)

しかし、特許文献1に記された離型剤供給装置では、圧送機構は中継室の底部側に塊状に堆積した離型剤を空気で送り出すことになるので、離型剤が均一な速度で連続的に圧送されず、キャビティ内に塗布される離型剤の厚さが不均一となる場合があった。その場合、離型剤の薄過ぎる箇所では成形品の焼き付きなどの問題が生じ、離型剤の厚過ぎる箇所では離型剤が成形品の表面に進入してガス化し、品質を低下させる虞があった。   However, in the release agent supply apparatus described in Patent Document 1, the pressure feeding mechanism sends out the release agent accumulated in a lump on the bottom side of the relay chamber with air, so that the release agent continues at a uniform speed. In some cases, the thickness of the release agent applied in the cavity is not uniform because the pressure is not pumped. In that case, if the release agent is too thin, problems such as seizure of the molded product may occur, and if the release agent is too thick, the release agent may enter the surface of the molded product and gasify, thereby reducing the quality. there were.

また、特許文献2に記された離型剤供給装置では、特許文献1に記された装置に比して離型剤が幾らか分散された状態での圧送を期待できるが、圧送用のエアの流量は容積の大きな拡散部にて急減するため、一部の離型剤が拡散部内で自由落下して拡散部の底部に堆積する場合があり、その結果、キャビティへの供給量が不安定となる傾向があった。また、比較的大きな拡散部を設ける必要があるため、圧送に際して多量のエアを供給することが必要である、また、拡散部を設けるための余分なスペースが必要である、などの点が未解決であった。   The release agent supply device described in Patent Document 2 can be expected to be pumped in a state in which the release agent is somewhat dispersed as compared with the device described in Patent Document 1, but the air for pumping is used. Since the flow rate of the liquid drops rapidly in the diffusion part with a large volume, some mold release agent may fall freely in the diffusion part and accumulate on the bottom of the diffusion part, resulting in unstable supply to the cavity. There was a tendency to become. In addition, since it is necessary to provide a relatively large diffusion part, it is necessary to supply a large amount of air when pumping, and an extra space for providing the diffusion part is still unsolved. Met.

そこで、本発明の目的は、上に例示した各従来技術が与える課題に鑑み、離型剤を均一な速度で連続的に圧送することができる離型剤供給装置を提供することにある。本発明の他の目的は、キャビティへの離型剤の供給量が安定し易く、また、比較的少量のエアで圧送を実施でき、装置全体をよりコンパクト化し易い離型剤供給装置を提供することにある。   Accordingly, an object of the present invention is to provide a release agent supply apparatus capable of continuously pumping a release agent at a uniform speed in view of the problems given by the conventional techniques exemplified above. Another object of the present invention is to provide a release agent supply device that can easily stabilize the supply amount of the release agent to the cavity, can carry out pressure feeding with a relatively small amount of air, and can make the entire device more compact. There is.

本発明による離型剤供給装置の第1の特徴構成は、
成形用モールドのキャビティに塗布する粉体状の離型剤を収納する離型剤タンクと、
前記キャビティと前記離型剤タンクとの間に設けられ、前記キャビティと連通した分散室と、
前記離型剤タンクから一定量の離型剤を抽出して前記分散室に供給する抽出装置と、
前記分散室に供給された離型剤を前記分散室内で分散化するアジテータ部と、
前記分散室内の離型剤を前記キャビティに空気で圧送する圧送機構と、
前記アジテータ部の駆動を制御すると共に、前記アジテータ部によって前記分散室内で離型剤が分散化している間に前記圧送機構の駆動をさせる制御装置と、を備え
前記アジテータ部は、前記分散室の下方に配置されていると共に、前記分散室の軸心から偏った位置に開口され、前記分散室内に空気流を供給する補助給気部を備え、
前記圧送機構は、前記分散室の上方に配置されていると共に、前記補助給気部から供給される空気流と逆向きの渦状の空気を供給すべく、前記分散室の軸心から偏った位置に開口されている主給気部からなる点にある。
The first characteristic configuration of the release agent supply apparatus according to the present invention is:
A release agent tank for storing a powder release agent to be applied to the cavity of the molding mold;
A dispersion chamber provided between the cavity and the release agent tank and in communication with the cavity;
An extraction device for extracting a predetermined amount of the release agent from the release agent tank and supplying it to the dispersion chamber;
An agitator for dispersing the release agent supplied to the dispersion chamber in the dispersion chamber;
A pumping mechanism for pumping the release agent in the dispersion chamber with air to the cavity;
A controller for controlling the driving of the agitator unit, and for driving the pumping mechanism while the release agent is dispersed in the dispersion chamber by the agitator unit ,
The agitator section is disposed below the dispersion chamber, and is opened at a position offset from the axis of the dispersion chamber, and includes an auxiliary air supply section that supplies an air flow into the dispersion chamber,
The pressure feeding mechanism is disposed above the dispersion chamber, and is deviated from the axis of the dispersion chamber so as to supply spiral air in the direction opposite to the air flow supplied from the auxiliary air supply unit. It is in the point which consists of the main air supply part opened in .

本発明の第1の特徴構成による離型剤供給装置では、分散室に供給された離型剤がアジテータ部によって攪拌、分散化され、離型剤が分散化している間に圧送されるので、離型剤が塊状にならず良く分散化したままの状態で圧送される。その結果、離型剤を均一な速度で連続的に圧送することができ(図4を参照)、また、キャビティへの離型剤の供給量も安定し易くなった(図5を参照)。さらに、特別に大容積の拡散部を設ける必要がないので、比較的少量のエアで圧送を実施でき、装置全体の大型化も抑制できる。
アジテータ部は、前記分散室内に分散用の空気流を供給する補助給気部を備えている。
このため、アジテータ部として例えばビーターのような機械的な分散化手段を用いた場合に比して、離型剤が付着・堆積する部品が少なくなるので、装置のメンテナンスが容易となる。
また、補助給気部は、前記分散室の下方に配置されている。
このため、分散室の下部から空気流を供給するすることができ、補助給気部が分散室の中間部や上部から離型剤に対して空気流を供給する構成に比して、比較的少なめの空気でも短時間で且つ効率的な分散化が得られる。
さらに、補助給気部は、前記分散室の軸心から偏った位置に開口されている。
このため、分散室内の内面に沿った左右いずれかの一定方向に回る渦状の空気流が発生するので、さらに効率的な分散化が得られる。
圧送機構は、前記分散室の上方に配置されていると共に、前記補助給気部から供給される空気流と逆向きの渦状の空気を供給すべく、前記分散室の軸心から偏った位置に開口されている主給気部からなる。
このため、主給気部から供給される空気流は、アジテータ部としての補助給気部によって形成された渦状の空気流とは逆の向きに回りながら下方に向かって進む渦を作るので、補助給気部によって分散化された離型剤の分散状態をさらに増大させながら分散室から送り出すことができる。
In the release agent supply apparatus according to the first characteristic configuration of the present invention, the release agent supplied to the dispersion chamber is stirred and dispersed by the agitator unit, and is sent while being released, The release agent is pumped in a state of being well dispersed without being agglomerated. As a result, the release agent can be continuously pumped at a uniform speed (see FIG. 4), and the supply amount of the release agent to the cavity is easily stabilized (see FIG. 5). Furthermore, since it is not necessary to provide a specially large volume diffusion section, it is possible to carry out the pressure feeding with a relatively small amount of air, and to suppress the enlargement of the entire apparatus.
The agitator section includes an auxiliary air supply section that supplies a dispersion air flow into the dispersion chamber.
For this reason, as compared with the case where a mechanical dispersing means such as a beater is used as the agitator section, the number of parts to which the release agent adheres and accumulates is reduced, and the maintenance of the apparatus is facilitated.
In addition, the auxiliary air supply unit is disposed below the dispersion chamber.
For this reason, it is possible to supply an air flow from the lower part of the dispersion chamber, and the auxiliary air supply unit is relatively free from the configuration in which the air flow is supplied to the release agent from the middle part or the upper part of the dispersion chamber. Even with a small amount of air, efficient dispersion can be obtained in a short time.
Further, the auxiliary air supply part is opened at a position deviated from the axis of the dispersion chamber.
For this reason, a vortex-like air flow that rotates in one of the left and right directions along the inner surface of the dispersion chamber is generated, so that more efficient dispersion can be obtained.
The pressure feeding mechanism is disposed above the dispersion chamber, and at a position deviated from the axis of the dispersion chamber so as to supply spiral air in the direction opposite to the air flow supplied from the auxiliary air supply unit. It consists of the main air supply part opened.
For this reason, the air flow supplied from the main air supply unit creates a vortex that moves downward while rotating in the opposite direction to the spiral air flow formed by the auxiliary air supply unit as the agitator unit. It can be sent out from the dispersion chamber while further increasing the dispersion state of the release agent dispersed by the air supply unit.

本発明の他の特徴構成は、前記分散室は、前記抽出装置と第1開閉弁を介して連通し、前記キャビティと第2開閉弁を介して連通した密閉空間であり、前記制御装置は、前記第1開閉弁および前記第2開閉弁を閉じた状態で前記アジテータ部を駆動させ、前記分散室内で離型剤が分散化している間に、前記第2開閉弁の開放と前記圧送機構の駆動とを実行させる点にある。   In another feature of the present invention, the dispersion chamber is a sealed space that communicates with the extraction device via a first on-off valve, and communicates with the cavity via a second on-off valve, and the control device includes: While the first on-off valve and the second on-off valve are closed, the agitator unit is driven, and while the release agent is dispersed in the dispersion chamber, the opening of the second on-off valve and the pumping mechanism It is in the point to perform driving.

本構成であれば、アジテータ部は第1開閉弁および第2開閉弁の閉鎖によって十分に密閉状態となった分散室で離型剤を分散化することになるので、アジテータ部による分散化によって一部の離型剤が抽出装置などへ逆流する虞がない。その結果、アジテータ部による急激な攪拌により短時間で十分な分散化を実現することが可能となる。   With this configuration, the agitator unit disperses the release agent in the dispersion chamber that is sufficiently sealed by closing the first on-off valve and the second on-off valve. There is no possibility that the release agent in the part flows backward to the extraction device or the like. As a result, it is possible to realize sufficient dispersion in a short time by rapid stirring by the agitator section.

本発明の他の特徴構成は、前記分散室は上方部の径が下方部の径よりも大きな、円錐面状を呈している点にある。   Another feature of the present invention is that the dispersion chamber has a conical surface shape in which the diameter of the upper part is larger than the diameter of the lower part.

本構成であれば、分散室の上方部に広めの空間が分散化のための空間として確保されるので、十分な分散化が得られ易い。また、分散室の底面が概して円錐面状を呈しているので、分散室から排出しきれない離型剤が分散室の底部に堆積する虞が少ない。   With this configuration, a wide space is secured as a space for dispersion above the dispersion chamber, so that sufficient dispersion can be easily obtained. In addition, since the bottom surface of the dispersion chamber is generally conical, the release agent that cannot be discharged from the dispersion chamber is less likely to accumulate on the bottom of the dispersion chamber.

本発明による離型剤供給装置を射出成形装置と共に示す略図である。1 is a schematic view showing a release agent supply apparatus according to the present invention together with an injection molding apparatus. 分散室の横断面を示す断面図である。It is sectional drawing which shows the cross section of a dispersion chamber. 離型剤供給装置の各状態と対応する工程とを示す説明図である。It is explanatory drawing which shows the process corresponding to each state of a mold release agent supply apparatus. 経過時間毎の離型剤通過量の測定結果を示すグラフである。It is a graph which shows the measurement result of the mold release agent passage amount for every elapsed time. 離型剤搬出量の測定結果を示すグラフである。It is a graph which shows the measurement result of a mold release agent carrying amount.

以下に本発明を実施するための形態について図面を参照しながら説明する。
図1は、本発明による離型剤供給装置を備えた射出成形装置の一例を示す。
この射出成形装置100は、固定型2aと可動型2bとを備えた金型2、金型2のキャビティVにアルミニウム合金などの溶湯を供給する給湯装置4、および、離型剤供給装置50を備える。可動型2bは着脱装置2cによって、固定型2aに密着された鋳造位置と、固定型2aから離間した離型位置との間で切り換え可能に支持されている。粉体離型剤としては、例えば、黒鉛、タルクなどの無機物粉体と、ワックス、樹脂、金属石鹸などの有機物粉体とを混合したものを用いることができる。
EMBODIMENT OF THE INVENTION Below, the form for implementing this invention is demonstrated, referring drawings.
FIG. 1 shows an example of an injection molding apparatus provided with a release agent supply apparatus according to the present invention.
The injection molding apparatus 100 includes a mold 2 having a fixed mold 2a and a movable mold 2b, a hot water supply apparatus 4 for supplying a molten metal such as an aluminum alloy to a cavity V of the mold 2, and a release agent supplying apparatus 50. Prepare. The movable mold 2b is supported by the attaching / detaching device 2c so as to be switchable between a casting position in close contact with the fixed mold 2a and a mold release position separated from the fixed mold 2a. As the powder release agent, for example, a mixture of inorganic powder such as graphite and talc and organic powder such as wax, resin and metal soap can be used.

給湯装置4は、固定型2aの一部に装着された給湯スリーブ5と、給湯スリーブ5に設けられた給湯口5aから溶湯を流し込むラドルなどからなる給湯容器(不図示)と、給湯スリーブ5に流し込まれた溶湯をキャビティVに押し出すプランジャ6とを備える。プランジャ6は油圧式のシリンダ(不図示)などによって往復操作される。キャビティVの上方に連通配置されたオーバーフロー部、オーバーフロー部の上端に連通しているガス抜き孔、金型2を冷却するための冷却装置などは図から省略されている。   The hot water supply device 4 includes a hot water supply sleeve 5 attached to a part of the fixed mold 2 a, a hot water supply container (not shown) made of a ladle or the like for pouring molten metal from a hot water supply port 5 a provided in the hot water supply sleeve 5, and a hot water supply sleeve 5. And a plunger 6 for pushing out the poured molten metal into the cavity V. The plunger 6 is reciprocated by a hydraulic cylinder (not shown) or the like. An overflow portion communicating with the cavity V, a gas vent hole communicating with the upper end of the overflow portion, a cooling device for cooling the mold 2, and the like are omitted from the drawing.

(離型剤供給装置の概略構成)
離型剤供給装置50は、キャビティVの内面に塗布する粉体状の離型剤を収納する離型剤タンク7と、離型剤タンク7から一定量の離型剤を抽出する抽出装置12と、抽出装置12によって抽出された離型剤を一旦受け入れる中継容器13と、中継容器13からキャビティVまで延びた離型剤供給パイプ15とを有する。
(Schematic configuration of release agent supply device)
The release agent supply device 50 includes a release agent tank 7 that stores a powder release agent to be applied to the inner surface of the cavity V, and an extraction device 12 that extracts a predetermined amount of the release agent from the release agent tank 7. And a relay container 13 for once receiving the release agent extracted by the extraction device 12 and a release agent supply pipe 15 extending from the relay container 13 to the cavity V.

離型剤タンク7の下部には漏斗状の絞り部7aが設けられている。この絞り部7aの周面には、内部の離型剤による架橋形成をエア供給によって防止するための複数の第1給気口N1が配置されている。
離型剤タンク7と抽出装置12とは、上下に延びた第1接続管8aによって接続されている。この第1接続管8aには、第1接続管8aの内部を閉塞した離型剤を逆洗するための第2給気口N2が配置されている。
抽出装置12は横向きに延びたシリンダ9と、シリンダ9の内部を油圧操作機構9aによって往復摺動操作されるピストン10とを備えている。ピストン部10には離型剤を受け入れるための縦穴10aが貫通形成されている。
A funnel-shaped throttle portion 7 a is provided at the lower part of the release agent tank 7. A plurality of first air supply ports N1 are arranged on the peripheral surface of the throttle portion 7a to prevent the formation of cross-linking by the internal release agent by supplying air.
The release agent tank 7 and the extraction device 12 are connected by a first connection pipe 8a extending vertically. The first connection pipe 8a is provided with a second air supply port N2 for backwashing the release agent that has closed the inside of the first connection pipe 8a.
The extraction device 12 includes a cylinder 9 extending in the lateral direction and a piston 10 that is reciprocally slid inside the cylinder 9 by a hydraulic operation mechanism 9a. The piston part 10 is formed with a vertical hole 10a for receiving a release agent.

抽出装置12と中継容器13とは、上下に延びた直管状の第2接続管8bによって連通接続されている。この第2接続管8bには、離型剤の通過を制御する第1開閉弁PV1が配置されている。
抽出装置12のピストン部10は、縦穴10aが上流側の離型剤タンク7とのみ連通する受け入れ位置と、縦穴10aが下流側の第2接続管8bとのみ連通する供給位置との間で往復操作される。
また、第1接続管8aと対向するシリンダ9の内面には、縦穴10a内の離型剤を空気によって下方に送り出すための第3給気口N3が配置されている。
The extraction device 12 and the relay container 13 are connected to each other by a straight tubular second connection pipe 8b extending vertically. A first on-off valve PV1 for controlling the passage of the release agent is disposed in the second connection pipe 8b.
The piston portion 10 of the extraction device 12 reciprocates between a receiving position where the vertical hole 10a communicates only with the upstream release agent tank 7 and a supply position where the vertical hole 10a communicates only with the second connecting pipe 8b on the downstream side. Operated.
Further, a third air supply port N3 for sending the release agent in the vertical hole 10a downward by air is disposed on the inner surface of the cylinder 9 facing the first connection pipe 8a.

中継容器13の内部には、概して下方から上方に向かって内径が次第に拡大する円錐面状の内面を備えた分散室14が形成されている。分散室14の上端付近には、分散室14内の離型剤をキャビティVまで空気で圧送する圧送機構としての第4給気口N4(主給気部の一例)が配置されている。
分散室14の下端と離型剤供給パイプ15とは、上下に延びた直管状の第3接続管8cによって連通接続されている。この第3接続管8cには、離型剤の通過を制御する第2開閉弁PV2と、第2開閉弁PV2の上方に隣接した第5給気口N5が配置されている。
上方の第1開閉弁PV1と下方の第2開閉弁PV2とを閉鎖した状態では、分散室14は密閉空間を構成する。第5給気口N5(補助給気部の一例)は、分散室14に供給された離型剤を密閉された分散室14の内部で上方に舞い上がらせるようにして分散化するアジテータ部として機能することになる。
Inside the relay container 13, a dispersion chamber 14 having a conical inner surface whose inner diameter gradually increases from the lower side to the upper side is formed. Near the upper end of the dispersion chamber 14, a fourth air supply port N <b> 4 (an example of a main air supply unit) is disposed as a pressure feeding mechanism that pumps the release agent in the dispersion chamber 14 to the cavity V with air.
The lower end of the dispersion chamber 14 and the release agent supply pipe 15 are connected in communication by a third connecting pipe 8c having a straight tubular shape extending vertically. The third connecting pipe 8c is provided with a second on-off valve PV2 for controlling the passage of the release agent and a fifth air inlet N5 adjacent to the upper side of the second on-off valve PV2.
In a state where the upper first on-off valve PV1 and the lower second on-off valve PV2 are closed, the dispersion chamber 14 forms a sealed space. The fifth air supply port N5 (an example of the auxiliary air supply unit) functions as an agitator unit that disperses the release agent supplied to the dispersion chamber 14 so as to rise upward in the sealed dispersion chamber 14. Will do.

図2に示すように、第4給気口N4および第5給気口N5は、分散室14の軸心Xに向かって開口するのではなく、分散室14の内面に対する接線に沿うように開口されている。また、第4給気口N4と第5給気口N5とは、分散室14の軸心Xに対して逆の向きに偏心している。
図2の例では、第5給気口N5は軸心Xに対して左寄りに配置されているので、第5給気口N5から供給される空気流は、基本的に、上から見て時計方向に進む渦を作りながら、分散室14の底部寄りに位置する離型剤を、上方に向かって進む螺旋状の空気の流れによって舞い上げ、効率的に分散化させる。
As shown in FIG. 2, the fourth air supply port N <b> 4 and the fifth air supply port N <b> 5 do not open toward the axis X of the dispersion chamber 14 but open along a tangent to the inner surface of the dispersion chamber 14. Has been. Further, the fourth air supply port N4 and the fifth air supply port N5 are eccentric in the opposite directions with respect to the axis X of the dispersion chamber 14.
In the example of FIG. 2, the fifth air supply port N5 is arranged on the left side with respect to the axis X, so that the air flow supplied from the fifth air supply port N5 is basically a clock as viewed from above. While creating a vortex that progresses in the direction, the release agent located near the bottom of the dispersion chamber 14 is swept up by the spiral air flow that travels upward, and is efficiently dispersed.

他方、第4給気口N4は軸心Xに対して右寄りに配置されているので、第4給気口N4から供給される空気流は、基本的に、第5給気口N5から供給される空気流とは逆の、上から見て反時計方向で且つ下方に向かって進む渦を作る。したがって、螺旋状の空気の流れに既に舞い上がって分散化されている離型剤を、その分散状態をさらに増大させながら分散室から送り出すことができる。   On the other hand, since the fourth air supply port N4 is disposed on the right side with respect to the axis X, the air flow supplied from the fourth air supply port N4 is basically supplied from the fifth air supply port N5. This creates a vortex that travels counterclockwise and downward as seen from above, opposite to the air flow. Accordingly, the release agent that has already been dispersed in the spiral air flow can be sent out from the dispersion chamber while further increasing the dispersion state.

前述した第1から第5の各給気口N1,N2,N3,N4,N5は後述する弁制御部81によって開閉操作される開閉弁および流量調整弁(不図示)を介して共通の圧縮空気源30に接続されている。アジテータ部として設けた第5給気口N5による空気流の圧力は、圧送機構として設けた第4給気口N4による空気流の圧力の十分の一以下でよい。
分散室14の内径は、最大内径箇所である上端部でも離型剤供給パイプ15の内径の2倍以下に設定されているので、第4給気口N4による空気流の流速が分散室14の内部で小さくなる虞が少ない。尚、分散室14の内部の適切な上下長さは、1回で供給すべき離型剤の量が20g以下の場合、例えば200mmとすればよい。
The first to fifth air supply ports N1, N2, N3, N4, and N5 described above are commonly compressed air via an on-off valve and a flow rate adjusting valve (not shown) that are opened and closed by a valve control unit 81 described later. Connected to the source 30. The pressure of the air flow through the fifth air supply port N5 provided as the agitator may be one tenth or less of the pressure of the air flow through the fourth air supply port N4 provided as the pressure feeding mechanism.
Since the inner diameter of the dispersion chamber 14 is set to be not more than twice the inner diameter of the release agent supply pipe 15 even at the upper end portion which is the maximum inner diameter portion, the flow velocity of the air flow through the fourth air supply port N4 is There is little possibility of becoming small inside. Note that the appropriate vertical length inside the dispersion chamber 14 may be, for example, 200 mm when the amount of the release agent to be supplied at one time is 20 g or less.

尚、可動金型2bの内部まで延びた離型剤供給パイプ15の終端部とキャビティVとの間には、離型剤供給パイプ15とキャビティVとを接続する入力ポート18aと、この入力ポートを開閉制御可能な供給シャットオフピン19aが設けられている。他方、固定金型2aには、キャビティVの一部を大気と連通させる排気ポート18bと、この排気ポート18bを開閉制御可能な排出シャットオフピン19bが設けられている。供給シャットオフピン19aおよび排出シャットオフピン19bは金型内に設けられたソレノイドによって開閉操作される。排気ポート18bにはキャビティVから排出された余分な離型剤を回収する回収装置を連通接続することができる。   An input port 18a for connecting the release agent supply pipe 15 and the cavity V between the end portion of the release agent supply pipe 15 extending to the inside of the movable mold 2b and the cavity V, and this input port A supply shut-off pin 19a that can be controlled to be opened and closed is provided. On the other hand, the fixed mold 2a is provided with an exhaust port 18b for allowing a part of the cavity V to communicate with the atmosphere, and an exhaust shut-off pin 19b capable of controlling the opening and closing of the exhaust port 18b. The supply shutoff pin 19a and the discharge shutoff pin 19b are opened and closed by a solenoid provided in the mold. A recovery device that recovers excess release agent discharged from the cavity V can be connected to the exhaust port 18b.

図2に示すように、この射出成形装置100はコントロールユニット70(制御装置の一例)を含む。このコントロールユニット70は鋳造装置100の各種制御要素を制御する機能を有する。このため、このコントロールユニット70は、コンピュータシステムとして構成されている。コントロールユニット70には、本発明に特に関係する出力デバイスとして、第1から第5の各給気口N1−N5を開閉制御する各アクチュエータ、および、第1開閉弁PV1と第2開閉弁PV2を開閉制御する各アクチュエータなどが接続されている。   As shown in FIG. 2, the injection molding apparatus 100 includes a control unit 70 (an example of a control apparatus). The control unit 70 has a function of controlling various control elements of the casting apparatus 100. For this reason, the control unit 70 is configured as a computer system. The control unit 70 includes, as output devices particularly related to the present invention, actuators that control the opening and closing of the first to fifth air supply ports N1-N5, and the first on-off valve PV1 and the second on-off valve PV2. Each actuator that controls opening and closing is connected.

各種入力デバイスから入力された操作信号を処理して、要求される出力信号を各種出力デバイスに出力するため、コントロールユニット70には、実質的にはプログラムとプログラム実行デバイスからなる制御部80が備えられている。この制御部80における特に本発明に関係する機能部は、上記合計7個の各開閉弁の開閉制御を実行する弁制御部81と、抽出装置12を駆動制御する抽出制御部82と、弁制御部の操作に基づいてシャットオフピン19a,19bの開閉制御を実行するピン制御部83である。これらの弁制御部81と抽出制御部82とピン制御部83による制御は、基本的に給湯装置4のプランジャ6の動きに基づいて決定される鋳造(射出成形)動作のスケジュールに沿って実行される。   In order to process operation signals input from various input devices and output required output signals to the various output devices, the control unit 70 includes a control unit 80 that is substantially composed of a program and a program execution device. It has been. In the control unit 80, the functional unit particularly related to the present invention includes a valve control unit 81 that performs opening / closing control of each of the seven on-off valves, an extraction control unit 82 that drives and controls the extraction device 12, and valve control The pin control unit 83 executes opening / closing control of the shut-off pins 19a and 19b based on the operation of the unit. The control by the valve control unit 81, the extraction control unit 82, and the pin control unit 83 is executed in accordance with a casting (injection molding) operation schedule that is basically determined based on the movement of the plunger 6 of the hot water supply device 4. The

(離型剤供給装置の動作)
本発明による離型剤供給装置50の動作について、射出成形装置100の動作に沿って説明する。
先ず、基本的な射出成形装置100による1回の鋳造(射出成形)動作は、可動型2bを固定型2aに密着固定する「型閉め」工程、離型剤供給装置50によってキャビティVに離型剤を圧送する「(離型剤)圧送」工程、給湯口5aから給湯スリーブ4にアルミ合金などの溶湯を流し込む「給湯」工程、プランジャ6で溶湯を金型2のキャビティVに送り出し、プランジャ6による圧力を保持する「射出充填工程」、金型2を冷却手段(不図示)で冷却することでキャビティVの溶湯を凝固させる「凝固/成形」工程、凝固完了後に可動型2bを移動して金型2を開放する「型開き」工程、成形品をイジェクトピン(不図示)などで可動型2bから押出す「成形品押出し」工程の手順で進められ、成形を連続的に進める場合は、次のショット(溶湯充填)のための「型閉め」工程に戻る。
(Operation of release agent supply device)
The operation of the mold release agent supply device 50 according to the present invention will be described along the operation of the injection molding device 100.
First, a single casting (injection molding) operation by the basic injection molding apparatus 100 is a "mold closing" process in which the movable mold 2b is closely fixed to the fixed mold 2a, and the mold release agent supply apparatus 50 releases the mold into the cavity V. A “(release agent) pressure feeding” step of pumping the agent, a “hot water supply” step of pouring a molten metal such as an aluminum alloy from the hot water supply port 5 a into the hot water supply sleeve 4, and the plunger 6 sends out the molten metal to the cavity V of the mold 2. "Injection filling process" for maintaining the pressure by the "solidification / molding" process for solidifying the molten metal in the cavity V by cooling the mold 2 with cooling means (not shown), moving the movable mold 2b after completion of solidification When "mold opening" process to open the mold 2 and "molded product extrusion" process in which the molded product is pushed out from the movable mold 2b with an eject pin (not shown) etc. Next shot "Mold closing" for the (molten metal filling) Back to the process.

したがって、本発明の離型剤供給装置50による「(離型剤)圧送」工程は、「型閉め」工程と「給湯」工程との間の短時間の間に実施されるが、「(離型剤)圧送」工程を含む離型剤供給装置50による全体的な動作は、弁制御部81と抽出制御部82とピン制御部83とから出力される各信号によって、次の手順で進められる。   Therefore, the “(release agent) pressure feeding” step by the release agent supply device 50 of the present invention is performed in a short time between the “mold closing” step and the “hot water supply” step. The overall operation of the release agent supply device 50 including the “molding) pressure feeding” step is advanced in the following procedure by the signals output from the valve control unit 81, the extraction control unit 82, and the pin control unit 83. .

(装填工程)
図3(a)に示すように、抽出装置12のピストン10が押し出された後で、第2開閉弁PV2を閉位置に、第1開閉弁PV1を開位置に切り換え、第3給気口からブローエアが下向きに吹かれると、縦穴10a内の離型剤が中継容器13の分散室14に装填され、分散室14の下部に堆積される。
(Loading process)
As shown in FIG. 3A, after the piston 10 of the extraction device 12 is pushed out, the second on-off valve PV2 is switched to the closed position and the first on-off valve PV1 is switched to the open position, When blow air is blown downward, the release agent in the vertical hole 10 a is loaded into the dispersion chamber 14 of the relay container 13 and is deposited in the lower portion of the dispersion chamber 14.

(分散化工程)
次に、図3(b)に示すように、第1開閉弁PV1を閉位置に切り換え、分散室14の下部にある第5給気口N5(補助給気部、アジテータ部の一例)の開閉弁を開放すると、第5給気口N5から吹き込まれたエアによって、離型剤が攪拌を伴いながら上方に舞い上がり、離型剤は分散室14の内部で分散化させる。
尚、図3(b)に示すように、抽出装置12のピストン10は、分散化工程と平行して引退位置に戻しておくことができる。
(Dispersing process)
Next, as shown in FIG. 3B, the first on-off valve PV1 is switched to the closed position, and the fifth air supply port N5 (an example of the auxiliary air supply unit and the agitator unit) at the lower portion of the dispersion chamber 14 is opened and closed. When the valve is opened, the air blown from the fifth air supply port N5 causes the release agent to rise upward with stirring, and the release agent is dispersed inside the dispersion chamber 14.
In addition, as shown in FIG.3 (b), the piston 10 of the extraction apparatus 12 can be returned to the retraction position in parallel with the dispersion | distribution process.

(圧送工程)
次に、図3(c)に示すように、分散室14内での離型剤の分散化が継続中に、第2開閉弁PV2および第4給気口N4(主給気部)を同時に開位置に切り換えると、第4給気口N4から吹き込まれたエアによって、分散室14内で分散化された離型剤が離型剤供給パイプ15を介してキャビティVに圧送される。
因みに、離型剤のキャビティVへの進入を円滑にするために、供給シャットオフピン19aおよび排出シャットオフピン19bは、圧送工程の開始までに開位置に切り換えられている。
(Pressing process)
Next, as shown in FIG. 3C, the second on-off valve PV2 and the fourth air supply port N4 (main air supply unit) are simultaneously opened while the release agent is continuously dispersed in the dispersion chamber. When switched to the open position, the release agent dispersed in the dispersion chamber 14 is pumped to the cavity V via the release agent supply pipe 15 by the air blown from the fourth air supply port N4.
Incidentally, in order to smoothly enter the release agent into the cavity V, the supply shut-off pin 19a and the discharge shut-off pin 19b are switched to the open position by the start of the pumping process.

図3(c)に示すように、圧送工程と平行して、第1給気口N1と第2給気口N2とを数秒間だけ開放することで、離型剤タンク7または第1接続管8a内の離型剤を、次回のショットのために圧送する離型剤として、引退位置にあるピストン10の縦穴10a内に供給しておくことができる。
圧送工程が完了すると、供給シャットオフピン19aおよび排出シャットオフピン19bを閉位置に切り換えた後、「給湯」工程が実施される。
As shown in FIG. 3 (c), in parallel with the pressure feeding process, the release agent tank 7 or the first connection pipe is opened by opening the first supply port N1 and the second supply port N2 for only a few seconds. The release agent in 8a can be supplied into the vertical hole 10a of the piston 10 in the retracted position as a release agent to be pumped for the next shot.
When the pumping process is completed, after the supply shut-off pin 19a and the discharge shut-off pin 19b are switched to the closed position, the “hot water supply” process is performed.

尚、一般的な離型剤を用いる場合の一つの標準的な方法として、分散化工程における第5給気口N5からの給気継続期間は例えば0.1〜0.2秒間などの短時間とし、第4給気口N4からの給気開始のタイミングは、第5給気口N5からの給気開始から0.1〜0.3秒後とすれば、離型剤が分散化している間に圧送を行うことができる。   In addition, as one standard method in the case of using a general mold release agent, the supply duration from the fifth supply port N5 in the dispersion step is a short time such as 0.1 to 0.2 seconds. Assuming that the timing of the start of air supply from the fourth air supply port N4 is 0.1 to 0.3 seconds after the start of air supply from the fifth air supply port N5, the release agent is dispersed. Pumping can be performed in between.

但し、分散状態の継続期間は、第5給気口N5から供給される空気の流速、離型剤の粒径や量、分散室14内の形状や容積などによって左右される。したがって、第5給気口N5からの給気継続期間、および、圧送工程の開始タイミングの適正値は、事前に実験によって求めておくことが好ましい。   However, the duration of the dispersion state depends on the flow rate of air supplied from the fifth air supply port N5, the particle size and amount of the release agent, the shape and volume in the dispersion chamber 14, and the like. Therefore, it is preferable that the proper value of the supply air continuation period from the fifth air supply port N5 and the start timing of the pumping process is obtained in advance by experiments.

或いは、第5給気口N5からの給気継続期間の途中から圧送工程を開始する方法、或いは、圧送工程の終了まで第5給気口N5からの給気を継続する方法でも、離型剤が分散化している間での離型剤圧送を行うことができる。   Alternatively, the mold release agent may be a method of starting the pressure feeding process from the middle of the air supply continuation period from the fifth air supply port N5, or a method of continuing air supply from the fifth air supply port N5 until the end of the pressure feeding process. The mold release agent can be fed while is dispersed.

本発明の実施例として、本発明による離型剤供給装置50を用いて離型剤をキャビティVに供給した場合の離型剤通過量の測定結果の例(図4)、および、キャビティVに供給された離型剤の離型剤搬出量の測定結果の例(図5)を示す。
尚、図4および図5には、比較例として、分散室なしの従来技術1(特許文献1に対応)と、分散室ありの従来技術2(特許文献2に対応)について同じ条件で測定した結果を併記している。
As an embodiment of the present invention, an example of the measurement result of the release agent passage amount when the release agent is supplied to the cavity V using the release agent supply device 50 according to the present invention (FIG. 4), and The example (FIG. 5) of the measurement result of the release agent delivery amount of the supplied release agent is shown.
In FIGS. 4 and 5, as a comparative example, measurement was performed under the same conditions for Conventional Technology 1 without a dispersion chamber (corresponding to Patent Document 1) and Conventional Technology 2 with a dispersion chamber (corresponding to Patent Document 2). The results are also shown.

(離型剤通過量)
先ず、図4に示す離型剤通過量は、離型剤供給装置から圧送されて或る地点を通過した離型剤の質量を、離型剤供給パイプ15の特定位置(図1にYで示す)に設置した静電容量型の粉体通過量センサ(不図示)で測定した結果であり、横軸は圧送開始時点からの経過時間を示し、縦軸はY地点を通過した離型剤の質量を示す。
(Amount of release agent passed)
First, the release agent passage amount shown in FIG. 4 is obtained by calculating the mass of the release agent that has been pressure-fed from the release agent supply device and passed through a certain point by the specific position of the release agent supply pipe 15 (Y in FIG. 1). The horizontal axis indicates the elapsed time from the start of pumping, and the vertical axis indicates the release agent that has passed through the Y point. The mass of

図4に示された結果を見ると、分散室なしの従来技術1(二点鎖線)の装置では、経過時間の早期に急激な立ち上がりと、それに続く非常に高い略単一のピークが見られ、曲線の裾野の広がりは比較的狭い。これは、圧送開始から短い時間に著しく急激な離型剤の通過が行われ、非常に短い時間で通過が終了していることを示している。したがって、中継容器の離型剤が塊状に近い状態で送り出されたことが推測される。   When the result shown in FIG. 4 is seen, in the apparatus of the prior art 1 (two-dot chain line) without the dispersion chamber, a rapid rise in the early stage of the elapsed time and the subsequent very high substantially single peak can be seen. The base of the curve is relatively narrow. This indicates that the release agent is remarkably abruptly passed in a short time from the start of pumping, and the passage is finished in a very short time. Therefore, it is estimated that the release agent of the relay container was sent out in a state close to a lump.

次に、分散室ありの従来技術2(細い実線)の装置では、従来技術1よりも大きく遅れた立ち上がりと、それに続く従来技術1ほどには高くないピークが見られ、曲線の裾野の広がりは従来技術1よりも広い。したがって、中継容器の離型剤が従来技術1の場合よりも分散された状態で送り出されたこと、また、中継容器内の離型剤が少なくなってからは非常に少量ずつの供給が長く続いたことが推測される。また、従来技術1と同様に、略単一のピークしか見られないため、圧送中における通過量の均一性が十分ではなかったことが推測される。   Next, in the apparatus of the conventional technique 2 (thin solid line) with a dispersion chamber, a rise that is greatly delayed from the conventional technique 1 and a subsequent peak that is not as high as that of the conventional technique 1 are seen. It is wider than the prior art 1. Therefore, the release agent in the relay container is sent out in a more dispersed state than in the case of the prior art 1, and after the release agent in the relay container is reduced, the supply in small quantities continues for a long time. I guess it was. Moreover, since only a substantially single peak is seen like the prior art 1, it is estimated that the uniformity of the passage amount during the pressure feeding was not sufficient.

他方、本発明(太い実線)による装置では、従来技術1に匹敵する早期の且つ急激な立ち上がりが見られ、それに続いて高さの揃った複数のピークが見られ、曲線の裾野の広がりは従来技術1と同等である。したがって、中継容器の離型剤が従来技術1、2のいずれの場合よりもよく分散された状態で送り出され、しかも、中継容器の離型剤の略全量が比較的短時間で圧送されたことが推測される。   On the other hand, in the apparatus according to the present invention (thick solid line), an early and abrupt rise comparable to that of the prior art 1 is observed, followed by a plurality of peaks having a uniform height, and the broadening of the base of the curve has been conventionally achieved. Equivalent to Technology 1. Therefore, the release agent of the relay container was sent out in a state of being better dispersed than in either of the prior art 1 and 2, and almost the entire amount of the release agent of the relay container was pumped in a relatively short time. Is guessed.

(離型剤搬出量)
図5に示す離型剤搬出量は、中継容器に供給された一定量の離型剤をキャビティに圧送させて、圧送から十分な時間が経過した時点でキャビティに到着している離型剤の質量
(搬出量)を測定するという操作を、各装置において20回繰り返し、この20回の測定結果の最小値と最大値と平均値とをプロットしたものである。装置毎に示された直線において、下端は最小値、上端は最大値、中間の黒丸は平均値を表す。
図5に示された結果を見ると、分散室ありの従来技術2の装置では、測定の度に搬出量が大きく異なる傾向が見られるが、本発明の装置では、分散室なしの従来技術1の装置と同様に略一定の搬出量が得られることがわかる。
(Amount of mold release agent)
The release agent delivery amount shown in FIG. 5 is that the fixed amount of release agent supplied to the relay container is pumped into the cavity, and when a sufficient time has passed since the pumping, The operation of measuring the mass (carrying amount) is repeated 20 times in each apparatus, and the minimum value, maximum value, and average value of the measurement results of 20 times are plotted. In the straight line shown for each apparatus, the lower end represents the minimum value, the upper end represents the maximum value, and the middle black circle represents the average value.
When the result shown in FIG. 5 is seen, in the apparatus of the prior art 2 with the dispersion chamber, there is a tendency that the carry-out amount greatly differs for each measurement, but in the apparatus of the present invention, the prior art 1 without the dispersion chamber. It can be seen that a substantially constant carry-out amount can be obtained as in the case of the apparatus.

〔別実施形態〕
〈1〉アジテータ部としての補助給気部を構成する給気口は、必ずしも上記実施形態のように分散室14の下方に設ける必要はなく、例えば分散室14の上端付近に設けることも可能である。この場合、給気口として、分散室14の内周面に沿って下向きに開口した給気ノズルを同内周面に近接して設ければ高い分散効果が得られる。
[Another embodiment]
<1> The air supply port constituting the auxiliary air supply unit as the agitator unit is not necessarily provided below the dispersion chamber 14 as in the above-described embodiment, and can be provided, for example, near the upper end of the dispersion chamber 14. is there. In this case, a high dispersion effect can be obtained if an air supply nozzle that opens downward along the inner peripheral surface of the dispersion chamber 14 is provided close to the inner peripheral surface as the air supply port.

〈2〉上記の実施形態ではアジテータ部を、分散室14内の離型剤を空気流で分散する補助給気部によって構成しているが、離型剤を機械的に上方に撒き上げる羽根車やビーターを分散室14内に設け、これをアジテータ部として実施してもよい。 <2> In the above embodiment, the agitator section is constituted by the auxiliary air supply section that disperses the release agent in the dispersion chamber 14 by the air flow, but the impeller mechanically lifts the release agent upward. Alternatively, a beater may be provided in the dispersion chamber 14 and used as an agitator.

〈3〉分散化工程を行う際に、必ずしも分散室14を密閉空間とする必要はなく、例えば分散室14の上方を開閉する第1開閉弁PV1を開位置とした非密閉空間のまま分散化工程を行ってもよい。 <3> When performing the dispersion step, the dispersion chamber 14 does not necessarily have to be a sealed space. For example, the dispersion is performed in a non-sealed space in which the first on-off valve PV1 that opens and closes the dispersion chamber 14 is opened. You may perform a process.

〈4〉分散室14は必ずしも縦型とする必要はなく斜め或いは横型の配置とすることも可能である。 <4> The dispersion chamber 14 does not necessarily have to be a vertical type, and may be arranged obliquely or horizontally.

成形用モールドのキャビティに塗布する粉体状の離型剤を収納する離型剤タンクと、キャビティと連通した分散室と、離型剤タンクから一定量の離型剤を抽出して分散室に供給する抽出装置と、分散室に供給された離型剤を分散化するアジテータ部と、分散室内の離型剤をキャビティに圧送する圧送機構とを備えた、離型剤供給装置を改良する技術として利用可能である。   A release agent tank for storing a powder release agent to be applied to the mold cavity, a dispersion chamber communicating with the cavity, and extracting a predetermined amount of the release agent from the release agent tank into the dispersion chamber A technique for improving a release agent supply device, comprising: an extraction device to be supplied; an agitator that disperses the release agent supplied to the dispersion chamber; and a pumping mechanism that pumps the release agent in the dispersion chamber to the cavity. Is available as

N4 第4給気口(主給気部)
N5 第5給気口(補助給気部、アジテータ部)
PV1 第1開閉弁
PV2 第2開閉弁
V キャビティ
2 金型
7 離型剤タンク
10 ピストン
12 抽出装置
13 中継容器
14 分散室
15 離型剤供給パイプ
50 離型剤供給装置
70 コントロールユニット(制御装置)
80 制御部
81 弁制御部
82 抽出制御部
83 ピン制御部
100 射出成形装置
N4 4th air supply port (main air supply part)
N5 5th air supply port (auxiliary air supply part, agitator part)
PV1 1st on-off valve PV2 2nd on-off valve V Cavity 2 Mold 7 Release agent tank 10 Piston 12 Extraction device 13 Relay container 14 Dispersion chamber 15 Release agent supply pipe 50 Release agent supply device 70 Control unit (control device)
80 control unit 81 valve control unit 82 extraction control unit 83 pin control unit 100 injection molding apparatus

Claims (3)

成形用モールドのキャビティに塗布する粉体状の離型剤を収納する離型剤タンクと、
前記キャビティと前記離型剤タンクとの間に設けられ、前記キャビティと連通した分散室と、
前記離型剤タンクから一定量の離型剤を抽出して前記分散室に供給する抽出装置と、
前記分散室に供給された離型剤を前記分散室内で分散化するアジテータ部と、
前記分散室内の離型剤を前記キャビティに空気で圧送する圧送機構と、
前記アジテータ部の駆動を制御すると共に、前記アジテータ部によって前記分散室内で離型剤が分散化している間に前記圧送機構の駆動をさせる制御装置と、を備え
前記アジテータ部は、前記分散室の下方に配置されていると共に、前記分散室の軸心から偏った位置に開口され、前記分散室内に空気流を供給する補助給気部を備え、
前記圧送機構は、前記分散室の上方に配置されていると共に、前記補助給気部から供給される空気流と逆向きの渦状の空気を供給すべく、前記分散室の軸心から偏った位置に開口されている主給気部からなる離型剤供給装置。
A release agent tank for storing a powder release agent to be applied to the cavity of the molding mold;
A dispersion chamber provided between the cavity and the release agent tank and in communication with the cavity;
An extraction device for extracting a predetermined amount of the release agent from the release agent tank and supplying it to the dispersion chamber;
An agitator for dispersing the release agent supplied to the dispersion chamber in the dispersion chamber;
A pumping mechanism for pumping the release agent in the dispersion chamber with air to the cavity;
A controller for controlling the driving of the agitator unit, and for driving the pumping mechanism while the release agent is dispersed in the dispersion chamber by the agitator unit ,
The agitator section is disposed below the dispersion chamber, and is opened at a position offset from the axis of the dispersion chamber, and includes an auxiliary air supply section that supplies an air flow into the dispersion chamber,
The pressure feeding mechanism is disposed above the dispersion chamber, and is deviated from the axis of the dispersion chamber so as to supply spiral air in the direction opposite to the air flow supplied from the auxiliary air supply unit. The mold release agent supply apparatus which consists of the main air supply part opened in .
前記分散室は、前記抽出装置と第1開閉弁を介して連通し、前記キャビティと第2開閉弁を介して連通した密閉空間であり、前記制御装置は、前記第1開閉弁および前記第2開閉弁を閉じた状態で前記アジテータ部を駆動させ、前記分散室内で離型剤が分散化している間に、前記第2開閉弁の開放と前記圧送機構の駆動とを実行させる請求項1に記載の離型剤供給装置。   The dispersion chamber is a sealed space communicating with the extraction device via a first on-off valve, and communicating with the cavity via a second on-off valve, and the control device includes the first on-off valve and the second on-off valve. The agitator section is driven with the on-off valve closed, and the second on-off valve is opened and the pumping mechanism is driven while the release agent is dispersed in the dispersion chamber. The mold release agent supply apparatus of description. 前記分散室は上方部の径が下方部の径よりも大きな、円錐面状を呈している請求項1又は2に記載の離型剤供給装置。 The dispersion chamber of the releasing agent supply device according to claim 1 or 2 diameter of the upper portion has the shape of a large, the conical shape than the diameter of the lower portion.
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