JP2006123202A - Casting machine and liquid substance supply method - Google Patents

Casting machine and liquid substance supply method Download PDF

Info

Publication number
JP2006123202A
JP2006123202A JP2004311034A JP2004311034A JP2006123202A JP 2006123202 A JP2006123202 A JP 2006123202A JP 2004311034 A JP2004311034 A JP 2004311034A JP 2004311034 A JP2004311034 A JP 2004311034A JP 2006123202 A JP2006123202 A JP 2006123202A
Authority
JP
Japan
Prior art keywords
circulation
discharge
pressure
mixing chamber
liquid
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.)
Withdrawn
Application number
JP2004311034A
Other languages
Japanese (ja)
Inventor
Toshiro Uchida
敏朗 内田
Hiroshi Hatanaka
拓 畑中
Akishi Inoue
晶司 井上
Kenichi Mochizuki
健一 望月
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.)
Canon Chemicals Inc
Original Assignee
Canon Chemicals Inc
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 Canon Chemicals Inc filed Critical Canon Chemicals Inc
Priority to JP2004311034A priority Critical patent/JP2006123202A/en
Publication of JP2006123202A publication Critical patent/JP2006123202A/en
Withdrawn legal-status Critical Current

Links

Images

Landscapes

  • Cleaning In Electrography (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a casting machine capable of casting a raw material liquid substance without exerting an effect on the material of a supply tank even if the temperature of the raw material liquid substance of the supply tank is set slightly lower and the temperature of the piping going toward a mixing chamber through a metering pump is set slightly higher in order to increase the reaction speed of a urethane, and a liquid substance supply method. <P>SOLUTION: In the casting machine having a route, which discharges a definite amount of the raw material liquid substance to the mixing chamber from the supply tank of the raw material liquid substance through piping by the metering pump, and a route for circulating the raw material liquid substance without discharging it to the mixing chamber, the circulating route has a liquid circulating confluent part between the supply tank and the metering pump. The liquid substance supply method is also disclosed. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、液状ウレタン樹脂等の原料液状物を定量ポンプにより、混合室に吐出させ、混合室にて混合させて金型に注入し、注入する必要のない時は定量ポンプを止めずに循環させている注型機及び液状物供給方法に関するものである。   In the present invention, a liquid material such as liquid urethane resin is discharged into a mixing chamber by a metering pump, mixed in the mixing chamber, poured into a mold, and circulated without stopping the metering pump when injection is not necessary. The present invention relates to a casting machine and a liquid supply method.

電子写真用ブレードは、複写機やプリンター等において転写後の感光体表面に付着した余分なトナーを除去するために(クリーニングブレード)、あるいは現像担持体に均一な膜厚のトナーを形成させるために(現像ブレード)用いられるが、これらブレードはポリウレタン等を原料として製造されている。すなわち、ポリウレタンの場合、イソシアネート成分からなる主剤とポリオール成分からなる硬化剤を注型機の供給タンクへ投入し、予熱、脱泡させた後、定量ポンプにより、混合室へ吐出し、混合攪拌した後に、その混合液を所定の金型内に注入し、所定の時間金型内にて硬化反応させて、脱型、切断させて上記クリーニングブレード等を得る。   The electrophotographic blade is used to remove excess toner adhering to the surface of the photoreceptor after transfer in a copying machine or printer (cleaning blade) or to form a toner having a uniform film thickness on the developing carrier. (Developing blades) are used, but these blades are manufactured using polyurethane or the like as a raw material. In other words, in the case of polyurethane, the main component consisting of an isocyanate component and the curing agent consisting of a polyol component are put into the supply tank of the casting machine, preheated and degassed, then discharged into the mixing chamber by a metering pump, and mixed and stirred. Thereafter, the mixed solution is poured into a predetermined mold, and is allowed to undergo a curing reaction in the mold for a predetermined time, and then demolded and cut to obtain the cleaning blade and the like.

ところで、上記ポリウレタンは上記金型に連続的に注入されてはいるものの、注型している金型と次に注型する金型とのタイムラグが生ずる場合は、ポリウレタンをロスショットしなければならず材料ロスにつながり、近年のローコスト化、排出物削減の流れに逆行するものとなる。また、この材料ロスをなくすべく定量ポンプを止めると、停止、開始の初期段階においては吐出量が安定せず主剤と硬化剤の比率が変化するという問題が発生する。特にクリーニングブレードの場合、この比率が変化すると、硬度や引っ張り特性等のウレタンゴム物性が変化し、すなわち、電子写真用として使用中にエッジ欠け、すり抜け等のクリーニング不良が発生する。そこで、特許文献1に記載のように、定量ポンプを止めることなく、吐出循環を繰り返し、更に、循環路内におけるタンクから混合室へ向かう往路側と混合室からタンクへ向かう復路側に圧力センサーを設けて吐出時と循環時の圧力を検出し制御する、という吐出方法が開示されている。   By the way, although the polyurethane is continuously injected into the mold, if there is a time lag between the casting mold and the next casting mold, the polyurethane must be shot in a loss. This leads to material loss and goes against the recent trend of lower costs and reduced emissions. Also, if the metering pump is stopped to eliminate this material loss, there is a problem that the discharge amount is not stable and the ratio of the main agent and the curing agent changes at the initial stage of stop and start. In particular, in the case of a cleaning blade, when this ratio changes, the urethane rubber properties such as hardness and tensile properties change, that is, defective cleaning such as edge chipping and slipping occurs during use for electrophotography. Therefore, as described in Patent Document 1, discharge circulation is repeated without stopping the metering pump, and pressure sensors are further provided on the forward path side from the tank to the mixing chamber in the circulation path and on the return path side from the mixing chamber to the tank. There is disclosed a discharge method of providing and detecting and controlling pressure during discharge and circulation.

また、近年のローコスト化のためには、金型へのウレタンの注入から脱型までの時間(硬化時間)を短くしてラインサイクルを短縮させることも必要になる。そのためには、硬化剤中に触媒を添加させて反応を早める方法(例えば、特許文献2)、金型の温度を高くする方法もあるが、硬化反応を早めるためには材料温度を高くすることも重要である。   In order to reduce the cost in recent years, it is also necessary to shorten the line cycle by shortening the time (curing time) from the injection of urethane into the mold to the demolding. For that purpose, there are a method of increasing the temperature of the mold by adding a catalyst to the curing agent (for example, Patent Document 2) and a method of increasing the temperature of the mold, but in order to accelerate the curing reaction, the material temperature must be increased. It is also important.

しかしながら、従来のタンクに向かう液状物供給方法だと、原料液状物投入初期に生産したブレードにおいては所定の硬度が得られるが、徐々にブレードの硬度が低下してくる、という問題が発生する。そこで、供給タンクの原料液状物温度を低めに設定し、定量ポンプを通して混合室へ向かう配管温度を高めに設定し、配管内で原料液状物温度を高め混合室内では高温で混合させることが望まれている。   However, according to the conventional liquid material supply method toward the tank, a predetermined hardness is obtained in the blade produced at the initial stage of starting the raw material liquid material, but there is a problem that the blade hardness gradually decreases. Therefore, it is desirable to set the raw material liquid temperature in the supply tank low, set the pipe temperature going to the mixing chamber through the metering pump high, and increase the raw material liquid temperature in the piping to mix at a high temperature in the mixing chamber. ing.

しかしながら、従来のタンクに戻る原料液状物循環型の注型機においては、混合室への吐出、タンクへの循環を繰り返すと、結局はタンク内の原料液状物温度も高温になってしまい、温度を別設定しても意味がなくなってしまう。
特開平6−210150号公報 (第5頁、図1) 特開2001−318569号公報 (第6頁、表1)
However, in the raw material liquid circulation type casting machine that returns to the conventional tank, if the discharge to the mixing chamber and the circulation to the tank are repeated, the temperature of the raw material liquid in the tank eventually becomes high. Even if another is set, the meaning is lost.
JP-A-6-210150 (5th page, FIG. 1) JP 2001-318569 A (Page 6, Table 1)

本発明の目的は、上述の点に鑑みなされたもので、ウレタンの反応速度を速めるため、供給タンクの原料液状物温度を低めに設定し、定量ポンプを通して混合室へ向かう配管温度を高めに設定しても、供給タンクの材料に影響を与えること無く、注型することが可能な、注型機及び液状物供給方法を提供することである。   The object of the present invention has been made in view of the above points, and in order to increase the reaction rate of urethane, the raw material liquid temperature of the supply tank is set lower, and the piping temperature toward the mixing chamber through the metering pump is set higher. Even so, it is an object of the present invention to provide a casting machine and a liquid material supply method capable of casting without affecting the material of the supply tank.

本発明に従って、原料液状物の供給タンクから配管を経由して定量ポンプにより一定量の該原料液状物を混合室に吐出する経路と、混合室へは吐出されずに循環する経路と、を有する注型機であって、該循環経路は、該供給タンクと該定量ポンプとの間に液循環合流部があることを特徴とする注型機が提供される。   According to the present invention, there are a path for discharging a predetermined amount of the liquid material from the raw material liquid supply tank to the mixing chamber by a metering pump via a pipe, and a path for circulating the liquid material without being discharged into the mixing chamber. A casting machine is provided, wherein the circulation path has a liquid circulation junction between the supply tank and the metering pump.

また、本発明に従って、原料液状物の供給タンクから配管を経由して定量ポンプにより一定量の該原料液状物を、混合室に吐出する液状物供給方法であって、以下の3つの工程、
(1)該供給タンクに設置した圧力センサーStの圧力値が、前記吐出循環ユニットに設置した圧力センサーScの該吐出循環ユニットの吐出循環切替バルブを循環に切り替えた際の圧力値より、小さく圧力調整する工程、
(2)該吐出循環ユニットの圧力値(Pc)と該供給タンクの圧力値(Pt)の圧力差(Pc−Pt)が0.01MPaより大きく1.5MPaより小さい値となるように設定する工程、
(3)該混合室への吐出と、該定量ポンプ側への循環への切り替える工程、
を含むことを特徴とする液状物供給方法が提供される。
Further, according to the present invention, there is provided a liquid supply method for discharging a predetermined amount of the raw material liquid material from the raw material liquid material supply tank to the mixing chamber by a metering pump via a pipe, and comprising the following three steps:
(1) The pressure value of the pressure sensor St installed in the supply tank is smaller than the pressure value when the discharge circulation switching valve of the discharge circulation unit of the pressure sensor Sc installed in the discharge circulation unit is switched to circulation. Adjusting process,
(2) A step of setting the pressure difference (Pc−Pt) between the pressure value (Pc) of the discharge circulation unit and the pressure value (Pt) of the supply tank to be a value larger than 0.01 MPa and smaller than 1.5 MPa. ,
(3) a step of switching to discharge to the mixing chamber and circulation to the metering pump side;
The liquid supply method characterized by including this is provided.

上記の構成を有する本発明の注型機及び液状物供給方法によれば、ウレタンの反応速度を速めるため、供給タンクの原料液状物温度を低めに設定し、定量ポンプを通して混合室へ向かう配管温度を高めに設定しても供給タンクと定量ポンプの間に液循環合流部があるため、供給タンクの材料に影響を与えること無く、注型することが可能な、注型機と液状物供給方法を提供することが可能となった。   According to the casting machine and the liquid supply method of the present invention having the above-described configuration, in order to increase the reaction rate of urethane, the raw material liquid temperature of the supply tank is set low, and the piping temperature toward the mixing chamber through the metering pump Casting machine and liquid material supply method that can be cast without affecting the material of the supply tank because there is a liquid circulation junction between the supply tank and the metering pump It became possible to provide.

本発明は、原料液状物の供給タンクから配管を経由して定量ポンプにより一定量の該原料液状物を混合室に吐出する経路と、混合室へは吐出されずに循環する経路と、を有する注型機において、該循環経路は、該供給タンクと該定量ポンプとの間に液循環合流部がある注型機である。そして、該循環経路には、該混合室への吐出と該定量ポンプ側への循環を切り替えるための吐出循環切替バルブと、圧力センサーと、圧力調整手段と、が配置してなり、これを吐出循環ユニットとしたものが複数形成されて、該混合室に吐出可能となるよう配置されたものである。   The present invention has a path for discharging a fixed amount of the raw material liquid material from the raw material liquid supply tank to the mixing chamber by a metering pump via a pipe, and a path for circulating the raw material liquid material without being discharged to the mixing chamber. In the casting machine, the circulation path is a casting machine having a liquid circulation merging portion between the supply tank and the metering pump. In the circulation path, a discharge circulation switching valve, a pressure sensor, and a pressure adjusting means for switching between discharge to the mixing chamber and circulation to the metering pump side are arranged, and this is discharged. A plurality of circulation units are formed and arranged so that they can be discharged into the mixing chamber.

以下に、本発明にかかる注型機への液状物供給方法を図1に基づいて説明する。   Below, the liquid substance supply method to the casting machine concerning this invention is demonstrated based on FIG.

図1は注型機にウレタンエラストマーを供給する装置の実施形態を示す全体図である。図1に示すように、注型機の吐出口よりウレタンエラストマーを金型に対して注入し、クリーニングブレードが成形される。   FIG. 1 is an overall view showing an embodiment of an apparatus for supplying urethane elastomer to a casting machine. As shown in FIG. 1, a urethane elastomer is injected into the mold from the discharge port of the casting machine, and a cleaning blade is formed.

本発明で使用する原料液状物は、主剤としてイソシアネート化合物(液状物A)と、硬化剤としてのポリオール化合物(液状物B)とをミキサーで混合した熱硬化性のウレタン樹脂液である。A系液状物及びB系液状物ともに、供給タンクからそれぞれ供給タンクの定量ポンプによって混合室へ吐出される。それぞれの原料液状物は、減圧下で脱泡した後、不活性ガスを用いてパージする。この時、不活性ガスとしては、窒素やアルゴン等を用いると良い。   The raw material liquid used in the present invention is a thermosetting urethane resin liquid in which an isocyanate compound (liquid A) as a main component and a polyol compound (liquid B) as a curing agent are mixed with a mixer. Both the A-system liquid material and the B-system liquid material are discharged from the supply tank to the mixing chamber by the metering pump of the supply tank. Each raw material liquid is degassed under reduced pressure and then purged with an inert gas. At this time, nitrogen, argon, or the like may be used as the inert gas.

供給タンク1と混合室17まで液送管2で、混合室17と液送管2の途中まで液戻管5で接続され、液送管2の途中に定量ポンプ6が介装されている。なお、ここで言う定量ポンプは、脈動が無く1回のパルスで定量の液が排出されるポンプであればよい。   A liquid feed pipe 2 connects the supply tank 1 and the mixing chamber 17, and a liquid return pipe 5 connects halfway between the mixing chamber 17 and the liquid feed pipe 2, and a metering pump 6 is interposed in the liquid feed pipe 2. The metering pump referred to here may be any pump that does not pulsate and discharges a metered liquid in one pulse.

供給タンク及び液送管は、常に一定温度に保温されている。一定温度とする手段としては、恒温層から定温水を蛇管等に流し該液送管に接触配置して行うこと、等が行われる。なお、供給タンクは、例えば、ステンレス製の概略円筒状で下部が円錐状になった構造が一般的であり、最下部から液が排出される。形状に関しては、原料液状物の滞留が生じない構造であればよい。   The supply tank and the liquid feed pipe are always kept at a constant temperature. As a means for keeping the temperature constant, for example, flowing constant temperature water from a constant temperature layer to a serpentine tube or the like and placing it in contact with the liquid feeding tube is performed. The supply tank generally has, for example, a generally stainless steel cylindrical shape with a conical lower portion, and the liquid is discharged from the lowermost portion. As for the shape, any structure that does not cause retention of the liquid raw material may be used.

次に、上記構成からなる注型機について、液状物供給方法を説明する。   Next, a liquid supply method for the casting machine having the above configuration will be described.

図1において、供給タンク1から液状物Aを定量ポンプ6により吐出循環切替バルブ4を介して混合室17へ吐出し、吐出する必要のない時は吐出循環切替バルブ4を切り替え液状物Aを液戻管5で液循環合流部7まで送り、定量ポンプ6により循環を繰り返す。再吐出時は、吐出循環切替バルブ4を切り替えればよい。   In FIG. 1, the liquid A is discharged from the supply tank 1 to the mixing chamber 17 via the discharge circulation switching valve 4 by the metering pump 6, and when there is no need to discharge, the discharge circulation switching valve 4 is switched and the liquid A is liquidated. It is sent to the liquid circulation junction 7 by the return pipe 5 and the circulation is repeated by the metering pump 6. What is necessary is just to switch the discharge circulation switching valve 4 at the time of re-discharge.

この際、供給タンクの圧力は不活性ガスで圧力(0.05MPa)を掛けており、液送管、ポンプまでは、この圧力値(Pt)で圧送される。該供給タンクの圧力は、液状物Aを液送管、ポンプまで圧送するのに十分な圧力であればよい。該供給タンク側に設置した圧力センサーStの圧力値(Pt)は、該吐出循環ユニットに設置した圧力センサーScの該吐出循環ユニットの該吐出・循環切替バルブを循環に切り替えた際の圧力値(Pc)より、小さいことが好ましい。そして、該供給タンク側の圧力値(Pt)が好ましくは0MPaより大きく0.1MPa以下、より好ましくは0.05〜0.1MPaであり、該吐出循環ユニットの圧力値(Pc)が好ましくは0.1〜1.5MPa、より好ましくは0.5〜1.0MPaであり、Pc−Ptが0.01MPaより大きく1.5MPaより小さい値であることが好ましい。この時、Pcが1.5MPaより高いと、混合室上部シールより液状物が漏れる恐れがある。定量ポンプ以降は圧力値を一定(0.01MPaより大きく1.5MPaより小さい値)になるように圧力調整手段を用いて調整する。   At this time, the pressure in the supply tank is an inert gas (0.05 MPa), and the liquid feed pipe and the pump are pumped at this pressure value (Pt). The pressure in the supply tank may be a pressure sufficient to pump the liquid A to the liquid feed pipe and the pump. The pressure value (Pt) of the pressure sensor St installed on the supply tank side is the pressure value when the discharge / circulation switching valve of the discharge circulation unit of the pressure sensor Sc installed on the discharge circulation unit is switched to circulation ( Smaller than Pc). The pressure value (Pt) on the supply tank side is preferably greater than 0 MPa and 0.1 MPa or less, more preferably 0.05 to 0.1 MPa, and the pressure value (Pc) of the discharge circulation unit is preferably 0. 0.1 to 1.5 MPa, more preferably 0.5 to 1.0 MPa, and Pc—Pt is preferably greater than 0.01 MPa and less than 1.5 MPa. At this time, if Pc is higher than 1.5 MPa, the liquid material may leak from the mixing chamber upper seal. After the metering pump, the pressure value is adjusted using a pressure adjusting means so that the pressure value becomes constant (a value larger than 0.01 MPa and smaller than 1.5 MPa).

吐出時においては、供給タンク1から液状物Aを液送管2で定量ポンプ6により混合室17へ送液され、混合された後、吐出ノズルより適量吐出される。しかし、該混合室への吐出と、該定量ポンプ側への循環に切り替える吐出循環切替バルブを循環側に切り替えた場合には、供給タンクの圧力値(Pt)が吐出循環ユニットの圧力値(Pc)より小さくなるように圧力調整し、その圧力差(Pc−Pt)が0.01MPaより大きく1.5MPaより小さい値の範囲となるので、液循環合流部において、液戻管で戻っている材料が優先的に循環され、再吐出時には循環を繰り返していた液状物から吐出される。   At the time of discharge, the liquid material A is fed from the supply tank 1 to the mixing chamber 17 by the metering pump 6 through the liquid feed pipe 2, mixed, and then discharged from the discharge nozzle in an appropriate amount. However, when the discharge circulation switching valve for switching to the discharge to the mixing chamber and the circulation to the metering pump side is switched to the circulation side, the pressure value (Pt) of the supply tank becomes the pressure value (Pc) of the discharge circulation unit. ) The pressure is adjusted to be smaller, and the pressure difference (Pc−Pt) is in the range of a value larger than 0.01 MPa and smaller than 1.5 MPa. Is preferentially circulated and discharged from a liquid material that has been circulated repeatedly during re-discharge.

吐出循環切替バルブは、極短時間の液回路の切り替えが行われる構造が選択される。また、塗料の液循環に用いられるものであるので、バルブの切り替え構造部での磨耗が無いか、極少ないことが要求される。従って、バルブの摺動機構部分の材質は、低摩耗性、或いは、高潤滑性の表面を有するものが好ましい。例えば、ポリテトラフルオロエチレン等のフッ素系樹脂、有機シラン等でコーティングされたものが挙げられる。   As the discharge circulation switching valve, a structure in which the liquid circuit is switched for a very short time is selected. In addition, since it is used for liquid circulation of paint, it is required that there is no or very little wear at the valve switching structure. Therefore, the material of the sliding mechanism portion of the valve is preferably one having a low wear or high lubricity surface. Examples thereof include those coated with a fluorine-based resin such as polytetrafluoroethylene and organic silane.

圧力調整手段は、吐出・循環切替バルブと液循環合流部の間に設けられ、循環時と吐出時の圧力が異なる場合に、前記吐出循環ユニットに設置した圧力センサーにおいて、吐出時の圧力値(Pd)と循環時の圧力(Pc)の差が好ましくは0.1MPa以下、より好ましくは0.05MPa以下になるよう調整を行う。本発明の事例としては、螺子調整のタイプを採用した。   The pressure adjusting means is provided between the discharge / circulation switching valve and the liquid circulation merging section. When the pressure at the time of circulation is different from the pressure at the time of discharge, the pressure sensor installed in the discharge circulation unit has a pressure value at the time of discharge ( Adjustment is performed such that the difference between Pd) and the pressure during circulation (Pc) is preferably 0.1 MPa or less, more preferably 0.05 MPa or less. As an example of the present invention, a screw adjustment type was adopted.

ところで、上記実施形態では、液状物Aの搬送方法のみ示したが、両方或いは片方のみに適用してもよい。   By the way, in the said embodiment, although only the conveyance method of the liquid A was shown, you may apply to both or only one side.

また、供給タンクの材料温度を低めに設定し、定量ポンプを通して混合室へ向かう間の配管温度を高めに設定し、混合室内では高温で反応させると、反応速度を増加させ、生産効率を上げることができる。このとき、本発明の循環方法を用いると原料劣化が少なくなる。   Also, if the material temperature of the supply tank is set low, the piping temperature is set high while going to the mixing chamber through the metering pump, and if the reaction is carried out at a high temperature in the mixing chamber, the reaction rate is increased and the production efficiency is increased. Can do. At this time, if the circulation method of the present invention is used, deterioration of the raw material is reduced.

実施例としては図1に示したような、該定量ポンプの前後を結ぶ経路が、循環路となるものであり、該循環路には、圧力センサーと、該混合室への吐出と、該定量ポンプ側への循環に切り替える吐出循環切替バルブと、圧力調整手段と、から構成されたものを用い、比較例としては図2に示したような循環の戻りが直接供給タンクに行くものを用いた。   As an example, a path connecting the front and rear of the metering pump as shown in FIG. 1 is a circulation path. The circulation path includes a pressure sensor, discharge into the mixing chamber, and the metering path. A discharge circulation switching valve that switches to circulation to the pump side and a pressure adjusting means is used. As a comparative example, the return of circulation as shown in FIG. 2 goes directly to the supply tank. .

(実施例1)
供給タンク内温度を60℃とし、混合室内原料温度を90℃、タンク圧力(Pt)0.05MPa、循環圧力(Pc)0.8MPa、吐出圧力(Pd)0.7MPaにして図1の注型装置を用いてウレタンを注型し、クリーニングブレードを作製した。
Example 1
The casting in FIG. 1 is performed at a supply tank temperature of 60 ° C., a mixing chamber raw material temperature of 90 ° C., a tank pressure (Pt) of 0.05 MPa, a circulation pressure (Pc) of 0.8 MPa, and a discharge pressure (Pd) of 0.7 MPa. Urethane was cast using an apparatus to prepare a cleaning blade.

(比較例1)
タンク内温度を90℃とし、混合室内原料温度を90℃、タンク圧力(Pt)0.05MPa、循環圧力(Pc)0.9MPa、吐出圧力(Pd)0.9MPaにして図2の注型装置を用いてウレタンを注型し、クリーニングブレードを作製した。
(Comparative Example 1)
The casting apparatus shown in FIG. 2 has a tank internal temperature of 90 ° C., a mixing chamber raw material temperature of 90 ° C., a tank pressure (Pt) of 0.05 MPa, a circulation pressure (Pc) of 0.9 MPa, and a discharge pressure (Pd) of 0.9 MPa. Urethane was cast using to prepare a cleaning blade.

(比較例2)
タンク内温度を60℃とし、混合室内原料温度を60℃、タンク圧力(Pt)0.05MPa、循環圧力(Pc)1.0MPa、吐出圧力(Pd)1.1MPaにして図2の注型装置を用いてウレタンを注型し、クリーニングブレードを作製した。
(Comparative Example 2)
The casting apparatus shown in FIG. 2 has a temperature in the tank of 60 ° C., a raw material temperature in the mixing chamber of 60 ° C., a tank pressure (Pt) of 0.05 MPa, a circulation pressure (Pc) of 1.0 MPa, and a discharge pressure (Pd) of 1.1 MPa. Urethane was cast using a to prepare a cleaning blade.

このようにして作製したクリーニングブレードについて、その製造過程の硬化脱型時間、エージング後の硬度を評価した。その結果を表1に示す。なお、上記特性の評価は以下のようにして行った。   The cleaning blade produced in this manner was evaluated for the curing and demolding time during the production process and the hardness after aging. The results are shown in Table 1. The above characteristics were evaluated as follows.

<硬化脱型時間>
原料混合物を130℃の成型型に注入、硬化反応させ、次いで硬化物を脱型するまでの時間を測定した。脱型するまでの時間の目安としては、脱型時の硬度で40°以上とした。
<Curing demolding time>
The raw material mixture was poured into a mold at 130 ° C. to cause a curing reaction, and then the time until the cured product was demolded was measured. As a measure of the time until demolding, the hardness at demolding was set to 40 ° or more.

<ブレード硬度>
液状物を供給タンクに投入し、注型を開始した直後、3時間後、12時間後にブレードをサンプリングし、1日間室温でエージングした後、ウレタンゴム硬度を測定した。なお、上記硬度(IRHD)の測定はウォーレス(H.W.WALLACE)社製ウォーレス微小硬度計を用い、JIS K 6253に基づいて行った。
<Blade hardness>
The liquid was put into the supply tank, and immediately after starting casting, the blade was sampled after 3 hours and 12 hours, and after aging at room temperature for 1 day, the urethane rubber hardness was measured. The hardness (IRHD) was measured based on JIS K 6253 using a Wallace microhardness meter manufactured by Wallace (HW WALLACE).

実施例と比較例の構成装置における原料液状物に対する影響を、ブレード硬度で評価した。原料投入初期に生産したブレードにおいては所定の硬度が得られるが、徐々にブレードの硬度が低下してくる。その硬度変化を、液循環方法の異なる2つの注型装置に対して検討した。   The influence on the raw material liquid in the constituent devices of Examples and Comparative Examples was evaluated by blade hardness. A predetermined hardness is obtained in the blade produced in the initial stage of charging the raw material, but the blade hardness gradually decreases. The change in hardness was examined for two casting apparatuses with different liquid circulation methods.

Figure 2006123202
Figure 2006123202

表1の結果より、実施例1では、混合室内原料温度をタンク内温度より上げると、反応速度が速くなり、脱型時間が1分と短くなる。更に、注型開始後3時間、12時間後の硬度変化がなかった。   From the results shown in Table 1, in Example 1, when the raw material temperature in the mixing chamber is raised from the temperature in the tank, the reaction rate is increased and the demolding time is shortened to 1 minute. Furthermore, there was no change in hardness after 3 hours and 12 hours after the start of casting.

一方、比較例1では、タンク内及び混合室内の温度を90℃に設定しており、反応速度は1分と速かったものの、硬度変化が大きかった。ここで、ブレード硬度が65°より低下すると、クリーニング不良となることが分かっている。また、比較例2では、タンク内及び混合室内の温度を60℃に設定しており、ブレードの硬度変化はなかったものの、反応速度が10分と遅かった。   On the other hand, in Comparative Example 1, the temperature in the tank and the mixing chamber was set to 90 ° C., and the reaction rate was as fast as 1 minute, but the hardness change was large. Here, it has been found that when the blade hardness falls below 65 °, cleaning failure occurs. Further, in Comparative Example 2, the temperature in the tank and the mixing chamber was set to 60 ° C., and the reaction rate was as slow as 10 minutes although there was no change in the hardness of the blade.

本発明にかかる注型機への液状物供給方法を説明する概略図である。It is the schematic explaining the liquid supply method to the casting machine concerning this invention. 従来の注型機への液状物供給方法を説明する概略図である。It is the schematic explaining the liquid supply method to the conventional casting machine.

1 供給タンクA
2 液送管
3 吐出液
4 吐出循環切替バルブ
5 液戻管
6 定量ポンプ
7 液循環合流部
8 圧力センサーSc
9 圧力調整ネジ
10 圧力センサーSt
11 供給タンクB
12 液送管
13 吐出循環切替バルブ
14 液戻管
15 定量ポンプ
16 ヘッドカバー
17 混合室
18 吐出口
19 液循環合流部
20 圧力センサーSc
21 圧力調整ネジ
22 圧力センサーSt
1 Supply tank A
2 Liquid feed pipe 3 Discharge liquid 4 Discharge circulation switching valve 5 Liquid return pipe 6 Metering pump 7 Liquid circulation junction 8 Pressure sensor Sc
9 Pressure adjusting screw 10 Pressure sensor St
11 Supply tank B
12 Liquid feed pipe 13 Discharge circulation switching valve 14 Liquid return pipe 15 Metering pump 16 Head cover 17 Mixing chamber 18 Discharge port 19 Liquid circulation confluence 20 Pressure sensor Sc
21 Pressure adjusting screw 22 Pressure sensor St

Claims (6)

原料液状物の供給タンクから配管を経由して定量ポンプにより一定量の該原料液状物を混合室に吐出する経路と、混合室へは吐出されずに循環する経路と、を有する注型機であって、該循環経路は、該供給タンクと該定量ポンプとの間に液循環合流部があることを特徴とする注型機。   A casting machine having a path for discharging a certain amount of the liquid material from the raw material liquid supply tank to the mixing chamber by a metering pump via a pipe and a path for circulating the liquid material without being discharged into the mixing chamber. The casting machine is characterized in that the circulation path has a liquid circulation junction between the supply tank and the metering pump. 前記循環経路には、前記混合室への吐出と循環を切り替えるための吐出循環切替バルブと、圧力センサーと、圧力調整手段と、が配置してなり、これを吐出循環ユニットとしたものが複数形成されて、前記混合室に吐出可能となるよう配置されている請求項1に記載の注型機。   In the circulation path, a discharge circulation switching valve for switching between discharge and circulation to the mixing chamber, a pressure sensor, and pressure adjusting means are arranged, and a plurality of discharge circulation units are formed. The casting machine according to claim 1, wherein the casting machine is disposed so as to be able to discharge into the mixing chamber. 前記供給タンクに設置した圧力センサーStの圧力値(Pt)が、前記吐出循環ユニットに設置した圧力センサーScの該吐出循環ユニットの前記吐出循環切替バルブを循環に切り替えた際の圧力値(Pc)より、小さい請求項1又は2に記載の注型機。   The pressure value (Pt) of the pressure sensor St installed in the supply tank is the pressure value (Pc) when the discharge circulation switching valve of the discharge circulation unit of the pressure sensor Sc installed in the discharge circulation unit is switched to circulation. The casting machine according to claim 1 or 2, which is smaller. 前記供給タンクの圧力値(Pt)が0MPaより大きく0.1MPa以下、前記吐出循環ユニットの圧力値(Pc)が0.1〜1.5MPaであり、Pc−Ptが0.01MPaより大きく1.5MPaより小さい値である請求項1〜3のいずれかに記載の注型機。   The pressure value (Pt) of the supply tank is greater than 0 MPa and 0.1 MPa or less, the pressure value (Pc) of the discharge circulation unit is 0.1 to 1.5 MPa, and Pc-Pt is greater than 0.01 MPa. The casting machine according to any one of claims 1 to 3, which has a value smaller than 5 MPa. 前記吐出循環ユニットに設置した圧力センサーにおいて、吐出時の圧力値(Pd)と循環時の圧力(Pc)の差が0.1MPa以下になるよう前記圧力調整手段により圧力調整した請求項4に記載の注型機。   The pressure sensor installed in the said discharge circulation unit WHEREIN: Pressure adjustment was carried out by the said pressure adjustment means so that the difference of the pressure value (Pd) at the time of discharge and the pressure (Pc) at the time of circulation might be 0.1 Mpa or less. Casting machine. 原料液状物の供給タンクから配管を経由して定量ポンプにより一定量の該原料液状物を、混合室に吐出する液状物供給方法であって、以下の3つの工程、
(1)該供給タンクに設置した圧力センサーStの圧力値(Pt)が、前記吐出循環ユニットに設置した圧力センサーScの該吐出循環ユニットの吐出循環切替バルブを循環に切り替えた際の圧力値(Pc)より、小さく圧力調整する工程、
(2)該吐出循環ユニットの圧力値(Pc)と該供給タンクの圧力値(Pt)の圧力差(Pc−Pt)が0.01MPaより大きく1.5MPaより小さい値となるように設定する工程、
(3)該混合室への吐出と、該定量ポンプ側への循環への切り替える工程、
を含むことを特徴とする液状物供給方法。
A liquid material supply method for discharging a certain amount of the raw material liquid material from the raw material liquid material supply tank to the mixing chamber by a metering pump via a pipe, comprising the following three steps:
(1) The pressure value (Pt) of the pressure sensor St installed in the supply tank is the pressure value when the discharge circulation switching valve of the discharge circulation unit of the pressure sensor Sc installed in the discharge circulation unit is switched to circulation ( Adjusting the pressure smaller than Pc),
(2) A step of setting the pressure difference (Pc−Pt) between the pressure value (Pc) of the discharge circulation unit and the pressure value (Pt) of the supply tank to be a value larger than 0.01 MPa and smaller than 1.5 MPa. ,
(3) a step of switching to discharge to the mixing chamber and circulation to the metering pump side;
The liquid supply method characterized by including.
JP2004311034A 2004-10-26 2004-10-26 Casting machine and liquid substance supply method Withdrawn JP2006123202A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004311034A JP2006123202A (en) 2004-10-26 2004-10-26 Casting machine and liquid substance supply method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004311034A JP2006123202A (en) 2004-10-26 2004-10-26 Casting machine and liquid substance supply method

Publications (1)

Publication Number Publication Date
JP2006123202A true JP2006123202A (en) 2006-05-18

Family

ID=36718404

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004311034A Withdrawn JP2006123202A (en) 2004-10-26 2004-10-26 Casting machine and liquid substance supply method

Country Status (1)

Country Link
JP (1) JP2006123202A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105834170A (en) * 2015-01-15 2016-08-10 深圳创怡兴实业有限公司 Cleaning strip and manufacturing method thereof
JP2019155843A (en) * 2018-03-16 2019-09-19 マツダ株式会社 Fluid material supply device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105834170A (en) * 2015-01-15 2016-08-10 深圳创怡兴实业有限公司 Cleaning strip and manufacturing method thereof
JP2019155843A (en) * 2018-03-16 2019-09-19 マツダ株式会社 Fluid material supply device
JP7098978B2 (en) 2018-03-16 2022-07-12 マツダ株式会社 Fluid material supply equipment

Similar Documents

Publication Publication Date Title
US11794409B2 (en) Resin distribution and maintenance system
KR101616306B1 (en) 3d printing apparatus for manufacturing cement product and mehtod thereof
JP5492746B2 (en) Blade member manufacturing method and apparatus for electrophotographic apparatus
JP2009073194A (en) Component mixing system
WO2004007172A8 (en) Process and apparatus for continuously producing an elatomeric composition
JP2006123202A (en) Casting machine and liquid substance supply method
JP2006293015A (en) Elastic roll and method for manufacturing same, electrophotographic process cartridge, and image forming apparatus having elastic roll
EP1313598B1 (en) Method and apparatus for compounding a heat cured rubber composition
KR100961057B1 (en) A Control Apparatus and the Same Method of Lading Temperature for Sheet Rubber
CN1159977A (en) Blade for electrophotographic devices and production method and production apparatus for same
JPH06210150A (en) Method for discharging liquid in mixer and the mixer
US5776395A (en) Method and apparatus for making a blade for electrophotographic devices
JP4982296B2 (en) Blade continuous manufacturing method and continuous manufacturing apparatus
KR101077881B1 (en) Liquid silicone many kinds injection system
JP2004243773A (en) Process for manufacturing polyurethane molding
KR101550384B1 (en) Micro LSR Injection Apparatus
JP4018033B2 (en) Blade material, manufacturing method and manufacturing apparatus thereof
JP5610957B2 (en) Method for producing polyurethane foam roller
JP2012192603A (en) Method and apparatus for manufacturing blade member
JP2006187940A (en) Manufacturing method of toner supply roller
JP5106550B2 (en) Foam extrusion molding equipment
JP2002219721A (en) Method for manufacturing seamless belt, and seamless belt
JP2021529247A (en) Reactive plastic manufacturing equipment and manufacturing method
JP4863338B2 (en) Urethane roller casting equipment
US20150266054A1 (en) Coating apparatus, and method for producing coating film

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20080108