JP2003170422A - Method for supplying mixing reaction curable material - Google Patents

Method for supplying mixing reaction curable material

Info

Publication number
JP2003170422A
JP2003170422A JP2001374461A JP2001374461A JP2003170422A JP 2003170422 A JP2003170422 A JP 2003170422A JP 2001374461 A JP2001374461 A JP 2001374461A JP 2001374461 A JP2001374461 A JP 2001374461A JP 2003170422 A JP2003170422 A JP 2003170422A
Authority
JP
Japan
Prior art keywords
agent
main agent
tank
main
supply
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001374461A
Other languages
Japanese (ja)
Inventor
Masakuni Nishino
正訓 西野
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.)
Honda Motor Co Ltd
Original Assignee
Honda Motor Co Ltd
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 Honda Motor Co Ltd filed Critical Honda Motor Co Ltd
Priority to JP2001374461A priority Critical patent/JP2003170422A/en
Publication of JP2003170422A publication Critical patent/JP2003170422A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/88Adding charges, i.e. additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/60Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
    • B29B7/603Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material in measured doses, e.g. proportioning of several materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/748Plants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7485Systems, i.e. flow charts or diagrams; Plants with consecutive mixers, e.g. with premixing some of the components
    • B29B7/749Systems, i.e. flow charts or diagrams; Plants with consecutive mixers, e.g. with premixing some of the components with stirring means for the individual components before they are mixed together
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/802Constructions or methods for cleaning the mixing or kneading device
    • B29B7/803Cleaning of mixers of the gun type, stream-impigement type, mixing heads
    • B29B7/805Cleaning of the mixing conduit, module or chamber part

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Accessories For Mixers (AREA)
  • Nozzles (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To supply a main agent of a mixing reaction curable material into a mixing chamber while reducing the mixing of air bubbles with the main agent, to make it possible to use a mixture obtained by the mixing with a curing agent without generating the adverse effect caused by the mixing with air bubbles, and to facilitate the control of a color to simply enable color changeover. <P>SOLUTION: A material supply line has a main agent tank 10, a curing agent tank 20 and an additive tank 30. The main agent based on a polyol is stored in the main agent tank 10, and an isocyanate compound of the curing agent is stored in the curing agent tank 20. An internal release agent and a colorant inferior to the compatibility with the polyol among the additives of the main agent are not compounded with the main agent, in order to prevent the mixing with air bubbles due to strong stirring and stored in the additive tank 30 as third supply components. These components are supplied to the mixing chamber of a spray gun through a line L3 separate from a main agent supply line L1a and a curing agent supply line L2a to mix the main agent, the curing agent, the internal release agent and the colorant. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【発明の属する技術分野】本発明は、混合反応硬化型材
料の供給方法に関する。
TECHNICAL FIELD The present invention relates to a method for supplying a mixed reaction curable material.

【従来の技術】従来より、ポリオールを主成分とする主
剤と、硬化剤のイソシアネート化合物とを使用した混合
反応硬化型材料が知られている。特開昭55−1339
34号には、この混合反応硬化型材料の混合室への供給
方法として、イソシアネート化合物からなる第1成分
と、活性水素化合物であるポリオール、着色剤、希釈
剤、内部離型剤、架橋剤、分散剤からなる主剤である第
2成分と、活性水素化合物と充填剤からなる第3成分と
を、それぞれの供給経路を通って成型機の混合室に供給
することが提案されている。上記公報は、混合反応硬化
型材料による樹脂成形品の製造方法に関するものである
が、樹脂成形品強化を目的としてガラス繊維等の充填剤
を配合しており、この充填剤を第1成分または第2成分
に配合すると、充填剤を配合された成分の粘度が著しく
増大して、高圧の圧送ポンプを使用する必要などの不都
合があることから、充填剤を第1成分または第2成分に
配合せずに、第3成分として独立に供給するように、材
料の供給方法を改良したものである。
2. Description of the Related Art Heretofore, a mixed reaction curable material has been known in which a main component containing a polyol as a main component and an isocyanate compound as a curing agent are used. JP-A-55-1339
No. 34, as a method of supplying the mixed reaction curable material to the mixing chamber, a first component composed of an isocyanate compound, a polyol which is an active hydrogen compound, a colorant, a diluent, an internal mold release agent, a crosslinking agent, It has been proposed to supply the second component, which is a main component composed of a dispersant, and the third component, which is composed of an active hydrogen compound and a filler, to the mixing chamber of the molding machine through the respective supply paths. The above-mentioned publication relates to a method for producing a resin molded product from a mixed reaction-curable material, which contains a filler such as glass fiber for the purpose of strengthening the resin molded product. When blended in two components, the viscosity of the component in which the filler is blended remarkably increases, and there is an inconvenience such as the necessity of using a high-pressure pressure pump. Therefore, the filler should not be blended in the first component or the second component. Instead, the material supply method is improved so that the third component is supplied independently.

【発明が解決しようとする課題】しかしながら、上記従
来の材料供給方法では、第2成分の主剤に、ポリオール
と比重や粘度が大きく異なる内部離型剤等の成分を含有
しているので、主剤を供給する主剤タンク内でこれらの
成分が分離しやすい。このため、主剤タンクでは貯蔵し
た主剤を強く攪拌することを要しており、この攪拌によ
り主剤中へ空気が巻き込れて、主剤に気泡の噛み込みが
発生する。ところで、混合反応硬化型材料の用途に表皮
成形があり、スプレーガンから主剤と硬化剤の混合物を
型内に噴霧して表皮を成形するように使用されるが、主
剤への気泡の噛み込みがあると、気泡の影響で混合物が
ノズルからスムースに出ず、ボテボテとした感じで噴霧
されて、型内に塗布された混合物の塗膜に粒子径のむら
が発生する。このため、従来は、得られる表皮成形品の
膜厚の不均一や色むらが生じる問題があった。また表皮
の伸びや強度の差異が激しく、確実に表皮成形品を剥離
できない問題を生じることもあった。本発明の課題は、
混合反応硬化型材料の主剤を気泡の噛み込みを低減して
混合室に供給でき、主剤と硬化剤との混合物を気泡の噛
み込みによる悪影響がない状態で使用に供することを可
能とした等の混合反応硬化型材料の供給方法を提供する
ことである。
However, in the above-mentioned conventional material supplying method, since the main component of the second component contains a component such as an internal release agent having a specific gravity and a viscosity greatly different from those of the polyol, the main component is not used. These components are easily separated in the main agent tank to be supplied. For this reason, it is necessary to strongly stir the stored main agent in the main agent tank, and this agitation causes air to be entrained in the main agent, causing air bubbles to be trapped in the main agent. By the way, there is skin forming as an application of the mixed reaction curing type material, and it is used to form a skin by spraying a mixture of a main agent and a curing agent into a mold from a spray gun. If so, the mixture does not come out smoothly from the nozzle due to the influence of air bubbles, and the mixture is sprayed with a fluffy feeling, resulting in uneven particle size in the coating film of the mixture applied in the mold. Therefore, conventionally, there has been a problem that the obtained skin-molded article has uneven film thickness and uneven color. In addition, the difference in elongation and strength of the skin is so great that it may cause a problem that the skin-molded article cannot be reliably peeled off. The object of the present invention is to
It is possible to supply the main agent of the mixed reaction curable material to the mixing chamber while reducing the entrapment of bubbles, and it is possible to use the mixture of the main agent and the curing agent in a state where there is no adverse effect due to the entrapment of bubbles. It is to provide a method for supplying a mixed reaction curable material.

【課題を解決するための手段】上記課題を解決するため
に、本発明は、混合反応硬化型材料の主剤と硬化剤と
を、それぞれの供給経路から混合室に供給する混合反応
硬化型材料の供給方法において、前記主剤の添加剤のう
ちの内部離型剤を主剤に配合せずに第3の供給成分とし
て、前記主剤および硬化剤の供給経路とは別の供給経路
から前記混合室に供給することを特徴とする。主剤の添
加剤である内部離型剤は、主剤の主成分であるポリオー
ルとの混和性が劣るが、内部離型剤を主剤と硬化剤の供
給経路とは別の供給経路から混合室に供給するようにし
て、主剤に内部離型剤を配合しておかなければ、主剤タ
ンク内では主剤を強く攪拌する必要がなく、主剤に空気
の巻き込みによる気泡の噛み込みが生じるのを低減でき
る。したがって、主剤と硬化剤とを混合した混合物を表
皮成形等に使用する際、気泡の噛み込みによる悪影響を
なくした状態で適用できる。これにより、例えば表皮成
形では、スプレーノズルから樹脂混合物をスムースに型
内に噴霧して塗布し、膜厚が均一等の良好な表皮を得る
ことが可能となる。この場合、主剤を用いて内部離型剤
を希釈しておけば、主成分のポリオールにより内部離型
剤に流動性を与えて、内部離型剤を液体と同様にポンプ
により圧送できる。また主剤の添加剤である着色剤もポ
リオールとの混和性が劣るので、第3の供給成分として
更に着色剤を内部離型剤に加えておくことができる。こ
のようにしておけば、混合反応硬化型材料の色の管理を
主剤を貯蔵する大きなタンクでせずに、内部離型剤を貯
蔵する小タンクで管理することができるので、材料の色
の管理が容易になる。
In order to solve the above-mentioned problems, the present invention provides a mixed reaction-curable material in which a main agent and a curing agent of the mixed-reaction-curable material are supplied to a mixing chamber from respective supply paths. In the supply method, the internal mold release agent among the additives of the main agent is supplied to the mixing chamber from a supply path different from the supply paths of the main agent and the curing agent as a third supply component without being mixed with the main agent. It is characterized by doing. The internal release agent, which is an additive for the main agent, has poor miscibility with the polyol, which is the main component of the main agent, but the internal release agent is supplied to the mixing chamber from a supply route different from the supply route of the main agent and the curing agent. As described above, if the main agent is not mixed with the internal release agent, it is not necessary to strongly stir the main agent in the main agent tank, and it is possible to reduce the occurrence of entrapment of air bubbles due to the entrainment of air in the main agent. Therefore, when a mixture obtained by mixing the main agent and the curing agent is used for skin forming or the like, it can be applied in a state in which the adverse effect due to the entrapment of bubbles is eliminated. Thus, for example, in skin molding, it is possible to smoothly spray the resin mixture into the mold from the spray nozzle and apply the resin mixture to obtain a good skin having a uniform film thickness. In this case, if the internal mold release agent is diluted with the main agent, the internal mold release agent can be fluidized by the polyol as the main component, and the internal mold release agent can be pumped by a pump like a liquid. Further, since the colorant, which is an additive of the main agent, also has poor miscibility with the polyol, a colorant can be further added to the internal release agent as the third supply component. By doing so, it is possible to manage the color of the mixed reaction curable material not with the large tank that stores the main agent, but with the small tank that stores the internal release agent. Will be easier.

【発明の実施の形態】以下、本発明の実施の形態を詳述
する。図1は、本発明の一実施の形態の供給方法を適用
した混合反応硬化型材料の供給ラインを示す説明図であ
る。本実施の形態では、混合反応硬化型材料は表皮成形
に使用する。図1に示すように、材料供給ラインは、主
剤タンク10と硬化剤タンク20と添加剤タンク30と
を有し、主剤タンク10は供給ラインL1aと戻りライ
ンL1bにより、硬化剤タンク20は供給ラインL2a
および戻りラインL2bにより、図示しない成型機に装
備した液体噴霧装置であるスプレーガンに接続されてい
る。添加剤タンク30は供給ラインL3によりスプレー
ガンに接続される。これら供給ラインL1a〜L3は管
路からなる。主剤タンク10はポリオールを主成分とす
る主剤を貯蔵しており、主剤タンク10には、主剤を攪
拌する攪拌機11と、熱媒をタンク10に循環して主剤
を加熱する、循環ポンプ16および温度調整用熱媒ヒー
タ17を介設した加熱循環路G1と、主剤タンク10内
の雰囲気を乾燥するエアードライアー9が取り付けられ
ている。主剤供給ラインL1aは主剤タンク10に取り
付けられ、この供給ラインL1aには、開閉バルブ18
と、タンク10から供給された主剤中の微細な異物を除
去するストレーナ12と、主剤の供給量を計量する計量
ポンプ13と、供給する主剤を加熱する熱交換器14
と、主剤の流量を計測する流量計15とが、この順に上
流側から介挿されている。混合室に供給される主剤の温
度は、流量計15下流の近くとスプレーガン近くの位置
で供給ラインL1aを流れる主剤の温度を液温計19で
測定して、測定温度に基づき熱交換器14での主剤の加
熱量を調節することにより所定温度に制御される。硬化
剤タンク20は硬化剤のイソシアネート化合物を貯蔵し
ており、硬化剤タンク20には、硬化剤を攪拌する攪拌
機21と、熱媒をタンク20に循環して硬化剤を加熱す
る、循環ポンプ26および温度調整用熱媒ヒータ27を
介設した加熱循環路G2とが取り付けられている。硬化
剤供給ラインL2aは硬化剤タンク20に取り付けら
れ、この供給ラインL2aには、主剤供給ラインL1a
と同様、開閉バルブ28と、タンク20から供給された
硬化剤中の微細な異物を除去するストレーナ22と、硬
化剤の供給量を計量する計量ポンプ23と、供給する硬
化剤を加熱する熱交換器24と、硬化剤の流量を計測す
る流量計25とが、この順に上流側から介挿されてい
る。混合室に供給される硬化剤の温度は、流量計25下
流の近くとスプレーガン近くの位置で供給ラインL2a
を流れる硬化剤の温度を液温計29で測定して、測定温
度に基づき熱交換器24での硬化剤の加熱量を調節する
ことにより所定温度に制御される。添加剤タンク30に
は、第1、第2の供給成分である主剤、硬化剤に対し、
従来、主剤に配合されている添加剤のうちの一部を第3
の供給成分として貯蔵している。この第3の供給成分
は、主剤の主成分であるポリオールと混和性が良好でな
い添加剤とし、本実施の形態では、第3の供給成分に内
部離型剤と着色剤(着色顔料)とを選択した。内部離型
剤および着色剤は、主剤のポリオールにより流動性を付
与して、液体と同様にポンプにより圧送可能にするため
に、主剤、好ましくは主成分のポリオールで希釈してタ
ンク30に収容する。添加剤供給ラインL3は主剤タン
ク30に取り付けられ、この供給ラインL3には定量ポ
ンプ31が介挿されている。供給ラインL3には、定量
ポンプ31の下流側で洗浄液タンク33が定量ポンプ3
4を介して接続される。表皮成形を実施するに当たり、
主剤タンク10では、貯蔵された主剤が攪拌機11によ
り攪拌され、温調用熱媒ヒーター17により所定温度に
温度調節されている。主剤には、主成分のポリオールと
比重や粘度が大きく異なり、ポリオールとの混和性が悪
い内部離型剤や着色剤の添加剤を配合していないので、
ポリオールと添加剤の分離を防ぐために強く攪拌する必
要がなく、軽度の攪拌を行えばよい。上記の攪拌および
温調下に、開閉バルブ28を開き、計量ポンプ13を作
動させて、主剤をタンク10から供給ラインL1aに送
り込む。供給ラインL1aに送り込まれた主剤は、スト
レーナ12で異物を濾し取られ、計量ポンプ13で供給
量(流量)を計量されながらラインL1aを圧送され、
スプレーガンに供給される。スプレーガンに供給された
主剤は、噴霧するとき以外はスプレーガンの混合室に入
らずに、戻りラインL1bを通って主剤タンク10に戻
され、主剤タンク→スプレーガン→主剤タンクと循環さ
れる。同様に、硬化剤タンク20でも、貯蔵された硬化
剤が攪拌機21により攪拌され、温調用熱媒ヒーター2
7により所定温度に温度調節されている。この攪拌およ
び温調下に、開閉バルブ28を開き、計量ポンプ23を
作動させて、硬化剤をタンク20から供給ラインL2a
に送り込む。供給ラインL2aに送り込まれた硬化剤
は、ストレーナ22で異物を濾し取られ、計量ポンプ2
3で供給量(流量)を計量されながらラインL2aを圧
送され、スプレーガンに供給される。スプレーガンに供
給された硬化剤は、主剤のときと同様、噴霧するとき以
外はスプレーガンの混合室に入らずに、戻りラインL2
bを通って硬化剤タンク20に戻され、硬化剤タンク→
スプレーガン→硬化剤タンクと循環される。噴霧時、ス
プレーガンに供給された主剤および硬化剤は混合室に噴
出され、噴出に伴う攪拌効果によって混合される。これ
と同時に、添加剤タンク30からの添加剤が混合室に噴
出され、主剤および硬化剤と混合される。添加剤は、定
量ポンプ31の作動によって供給ラインL3に送り込ま
れ、スプレーガンに圧送される。主剤、硬化剤および添
加剤(内部離型剤および着色剤)を混合することによっ
て得られた混合物は、スプレーガンの混合室からスプレ
ーノズルに圧送時の圧力で圧入され、ノズル先端のスプ
レーチップから型内に噴霧され、着色した表皮に成形さ
れる。表皮成形後、洗浄液タンク33から定量ポンプ3
4により洗浄液を供給ラインL3に流すことにより、供
給ラインL3およびスプレーガンの混合室等を洗浄する
ことができる。本実施の形態の供給方法は、以上のよう
に構成され、主剤の主成分であるポリオールとの混和性
が劣る添加剤である内部離型剤と着色剤とを主剤に配合
せず、第1、第2の供給成分の主剤と硬化剤に対し内部
離型剤および着色剤を第3の供給成分として、主剤と硬
化剤の供給経路とは別の供給経路からスプレーガンの混
合室に供給するようにしたので、主剤タンク内では主剤
を軽度に攪拌すればよくなって、主剤に空気の巻き込み
による気泡の噛み込みが生じるのを低減できる。したが
って、主剤と硬化剤(内部離型剤および着色剤の配合の
ない主剤と、硬化剤と内部離型剤および着色剤)を混合
した混合物を型内に噴霧して表皮成形するに際し、スプ
レーノズルから混合物を気泡の噛み込みによる悪影響が
ない状態でスムースに噴霧でき、型内に塗布された混合
物の塗膜に粒子径のむらが発生するのを防止できる。こ
のため、混合反応硬化型樹脂による膜厚が均一で色相が
明瞭な安定した表皮を得ることができる。また、表皮の
伸びや強度の差異が激しいために、表皮成形品が剥離し
にくくなるようなこともなく、確実に表皮成形品を剥離
することができる。さらに、着色剤を主剤に配合せずに
内部離型剤に加えてあるので、混合反応硬化型材料の色
の管理を主剤を貯蔵する大きなタンクでせずに、内部離
型剤および着色剤を貯蔵する小タンクで管理することが
できて、材料の色の管理が容易になる。本発明の他の実
施の形態を図2に示す。本実施の形態は、3色の添加剤
を貯蔵した添加剤タンク30a、30b、30cと、ス
プレーガンに供給する添加剤の色を切り替えるカラーチ
ェンジャー32とを備える点が、第一の実施の形態と相
違する。図2において、図1に付した符号と同一の符号
は同一の部材を示す。上記の添加剤タンク30a、30
b、30cには、仮にここでA色、B色、C色と定めた
着色剤(例えば黄色、赤色、青色)と、内部離型剤と
が、主剤、好ましくは主成分のポリオールで希釈して貯
蔵されている。添加剤タンク30a〜30cは、カラー
チェンジャー32にそれぞれ定量ポンプ31を介して接
続され、カラーチェンジャー32は供給ラインL3に接
続されている。カラーチェンジャー32には、さらに洗
浄液タンク33が定量ポンプ34を介して接続される。
噴霧時、カラーチェンジャー32により、供給ラインL
3と連結するタンク30a〜30cを切り換えることに
よって、スプレーガンに供給される添加剤の色が選択さ
れる。選択された色の添加剤は、そのタンクの定量ポン
プ31の作動により、カラーチェンジャー32を通って
供給ラインL3に送り込まれ、スプレーガンに圧送さ
れ、混合室に噴出される。そして第一の実施の形態のと
きと同様、タンク10、タンク20から供給ラインL1
a、L2aを通ってスプレーガンに供給され、混合室に
噴出された主剤および硬化剤と共に、噴出に伴う攪拌効
果によって混合される。主剤、硬化剤および添加剤(内
部離型剤および着色剤)の混合物は、同様に、スプレー
ノズル先端のチップから型内に噴霧され、着色した表皮
に成形される。表皮成形後、表皮成形する色を変えたい
場合には、洗浄液タンク33から定量ポンプ34により
洗浄液をカラーチェンジャー32を経て供給ラインL3
に流し、ラインL3およびスプレーガンの混合室等を洗
浄してから、所望の色の添加剤を選択して成形に使用す
ればよい。本実施の形態によれば、第一の実施の形態と
同様の効果を有する他、添加剤タンクを複数用意して複
数色の添加剤を切り換えて供給できるようにしたので、
混合反応硬化型材料の色を容易に変更することができる
利点もある。以上の実施の形態では、いずれも、主剤と
硬化剤のそれぞれの経路とは別の経路から供給する第3
の供給成分に、主剤の添加剤のうち内部離型剤と着色剤
を選択したが、内部離型剤および着色剤のうちの一方を
第3の供給成分としてもよく、さらには内部離型剤およ
び着色剤とは別な添加剤を第3の供給成分としてもよ
い。また実施の形態では、混合反応硬化型材料を表皮成
形に使用する場合の供給方法について説明したが、本発
明はこれに限られず、混合反応硬化型材料を塗料や射出
成形等の型成形に使用する場合の供給方法にも適用する
ことができる。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below. FIG. 1 is an explanatory diagram showing a supply line of a mixed reaction curable material to which a supply method according to an embodiment of the present invention is applied. In this embodiment, the mixed reaction-curable material is used for skin forming. As shown in FIG. 1, the material supply line includes a main agent tank 10, a curing agent tank 20, and an additive tank 30, the main agent tank 10 includes a supply line L1a and a return line L1b, and the curing agent tank 20 includes a supply line. L2a
And the return line L2b is connected to a spray gun which is a liquid spraying device equipped in a molding machine (not shown). The additive tank 30 is connected to the spray gun by a supply line L3. These supply lines L1a to L3 are formed of pipe lines. The main agent tank 10 stores a main agent containing a polyol as a main component. The main agent tank 10 includes a stirrer 11 for stirring the main agent, a circulation pump 16 for circulating a heat medium in the tank 10 to heat the main agent, and a temperature. A heating circuit G1 provided with an adjusting heat medium heater 17 and an air dryer 9 for drying the atmosphere in the main agent tank 10 are attached. The main agent supply line L1a is attached to the main agent tank 10, and an on-off valve 18 is provided in this supply line L1a.
A strainer 12 for removing fine foreign substances in the main agent supplied from the tank 10, a metering pump 13 for measuring the amount of the main agent supplied, and a heat exchanger 14 for heating the main agent to be supplied.
And a flow meter 15 for measuring the flow rate of the main agent are inserted in this order from the upstream side. Regarding the temperature of the main agent supplied to the mixing chamber, the temperature of the main agent flowing through the supply line L1a is measured near the downstream of the flow meter 15 and near the spray gun with the liquid thermometer 19, and the heat exchanger 14 is measured based on the measured temperature. The temperature is controlled to a predetermined temperature by adjusting the heating amount of the main agent. The curing agent tank 20 stores an isocyanate compound of a curing agent, and the curing agent tank 20 includes a stirrer 21 for stirring the curing agent and a circulation pump 26 for circulating a heat medium to the tank 20 to heat the curing agent. And a heating circulation path G2 having a temperature adjusting heat medium heater 27 interposed therebetween. The curing agent supply line L2a is attached to the curing agent tank 20, and the main agent supply line L1a is connected to this supply line L2a.
Similarly to the open / close valve 28, a strainer 22 for removing fine foreign matters in the curing agent supplied from the tank 20, a metering pump 23 for measuring the supply amount of the curing agent, and a heat exchange for heating the curing agent to be supplied. A container 24 and a flow meter 25 for measuring the flow rate of the curing agent are inserted in this order from the upstream side. The temperature of the curing agent supplied to the mixing chamber is the supply line L2a near the downstream of the flow meter 25 and near the spray gun.
The temperature of the curing agent flowing through the liquid is measured by the liquid thermometer 29, and the amount of heating of the curing agent in the heat exchanger 24 is adjusted based on the measured temperature to control the temperature to a predetermined temperature. In the additive tank 30, for the main agent and the curing agent, which are the first and second supply components,
Conventionally, some of the additives compounded in the main agent
It is stored as a supply ingredient of. This third supply component is an additive that is not well miscible with the polyol, which is the main component of the main component, and in the present embodiment, an internal release agent and a colorant (color pigment) are added to the third supply component. Selected. The internal mold release agent and the colorant are stored in the tank 30 after being diluted with the main agent, preferably the main component polyol, in order to impart fluidity with the main agent polyol and enable pumping like a liquid. . The additive supply line L3 is attached to the main agent tank 30, and a metering pump 31 is inserted in the supply line L3. In the supply line L3, the cleaning liquid tank 33 is provided on the downstream side of the metering pump 31.
4 are connected. In carrying out skin forming,
In the main agent tank 10, the stored main agent is agitated by a stirrer 11, and the temperature is adjusted to a predetermined temperature by a heating medium heater 17. Since the main component has a large difference in specific gravity and viscosity from the main component polyol, and does not contain additives such as internal mold release agents and colorants, which have poor miscibility with polyols,
In order to prevent the separation of the polyol and the additive, it is not necessary to stir vigorously, and mild stirring may be performed. Under the above stirring and temperature control, the open / close valve 28 is opened, the metering pump 13 is operated, and the main agent is sent from the tank 10 to the supply line L1a. The main agent sent to the supply line L1a is filtered by the strainer 12 to remove foreign matters, and the line L1a is pressure-fed while the supply amount (flow rate) is measured by the metering pump 13.
Supplied to the spray gun. The main agent supplied to the spray gun is returned to the main agent tank 10 through the return line L1b without entering the mixing chamber of the spray gun except when spraying, and is circulated as main agent tank → spray gun → main agent tank. Similarly, in the curing agent tank 20, the stored curing agent is agitated by the agitator 21, and the temperature control heating medium heater 2
The temperature is adjusted to a predetermined temperature by 7. Under this stirring and temperature control, the opening / closing valve 28 is opened, the metering pump 23 is operated, and the hardening agent is supplied from the tank 20 to the supply line L2a.
Send to. The hardening agent sent to the supply line L2a is filtered by a strainer 22 to remove foreign matter, and then the measuring pump 2
While the supply amount (flow rate) is being measured at 3, the line L2a is pressure-fed and supplied to the spray gun. The curing agent supplied to the spray gun does not enter the mixing chamber of the spray gun except when spraying, as in the case of the main agent, and returns to the return line L2.
Returned to the curing agent tank 20 through b, and the curing agent tank →
It is circulated from the spray gun to the hardener tank. During spraying, the main agent and the curing agent supplied to the spray gun are jetted into the mixing chamber and mixed by the stirring effect accompanying the jetting. At the same time, the additive from the additive tank 30 is jetted into the mixing chamber and mixed with the main agent and the curing agent. The additive is sent to the supply line L3 by the operation of the metering pump 31 and pressure-fed to the spray gun. The mixture obtained by mixing the main agent, curing agent, and additives (internal release agent and colorant) is pressed into the spray nozzle from the mixing chamber of the spray gun at the pressure when it is being pumped, and then sprayed from the spray tip at the tip of the nozzle. It is sprayed into a mold and molded into a colored skin. After forming the skin, the cleaning liquid tank 33 to the metering pump 3
By flowing the cleaning liquid to the supply line L3 by 4, it is possible to clean the supply line L3 and the mixing chamber of the spray gun. The supply method of the present embodiment is configured as described above, and does not mix the internal mold release agent and the colorant, which are additives having poor miscibility with the polyol, which is the main component of the main agent, in the main agent, , An internal release agent and a colorant as a third supply component to the main agent and the curing agent of the second supply component are supplied to the mixing chamber of the spray gun from a supply route different from the supply route of the main agent and the curing agent. Thus, the main agent only needs to be slightly agitated in the main agent tank, and it is possible to reduce the occurrence of air bubble entrapment due to air entrainment in the main agent. Therefore, when spraying the mixture of the main agent and the curing agent (the main agent without the combination of the internal release agent and the colorant, and the curing agent, the internal release agent and the colorant) into the mold, the spray nozzle is used. Therefore, the mixture can be smoothly sprayed in a state where there is no adverse effect due to the entrapment of air bubbles, and it is possible to prevent unevenness in particle diameter from occurring in the coating film of the mixture applied in the mold. Therefore, it is possible to obtain a stable skin having a uniform film thickness and a clear hue by the mixed reaction-curing resin. Further, since the difference in elongation and strength of the skin is large, the skin-molded article is not easily peeled off, and the skin-molded article can be reliably peeled off. Furthermore, since the colorant is added to the internal mold release agent without being blended with the main compound, it is possible to manage the color of the mixed reaction-curable material without using a large tank for storing the main compound. It can be managed in a small tank for storage, which makes it easy to control the color of the material. Another embodiment of the present invention is shown in FIG. The present embodiment is provided with additive tanks 30a, 30b, 30c storing additives of three colors and a color changer 32 for switching the colors of the additives supplied to the spray gun. Is different from. In FIG. 2, the same reference numerals as those shown in FIG. 1 indicate the same members. The above additive tanks 30a, 30
In b and 30c, a colorant (for example, yellow, red, blue) defined as A color, B color, and C color here and an internal mold release agent are diluted with a main component, preferably a main component polyol. Stored. The additive tanks 30a to 30c are connected to a color changer 32 via a metering pump 31, respectively, and the color changer 32 is connected to a supply line L3. A cleaning liquid tank 33 is further connected to the color changer 32 via a metering pump 34.
At the time of spraying, the supply line L is supplied by the color changer 32.
By switching the tanks 30a to 30c connected to No. 3, the color of the additive supplied to the spray gun is selected. The additive of the selected color is sent to the supply line L3 through the color changer 32 by the operation of the metering pump 31 of the tank, is pumped to the spray gun, and is jetted to the mixing chamber. Then, as in the case of the first embodiment, the tank 10 and the tank 20 are connected to the supply line L1.
a, L2a, is supplied to the spray gun, and is mixed with the main agent and the curing agent sprayed into the mixing chamber by the stirring effect accompanying the spraying. Similarly, the mixture of the main agent, the curing agent, and the additives (internal release agent and colorant) is sprayed into the mold from the tip of the spray nozzle tip to form a colored skin. When it is desired to change the color for forming the skin after forming the skin, the cleaning liquid is supplied from the cleaning liquid tank 33 through the color changer 32 by the metering pump 34 to the supply line L3.
Then, the line L3, the mixing chamber of the spray gun and the like are washed, and then an additive having a desired color is selected and used for molding. According to the present embodiment, in addition to having the same effect as the first embodiment, a plurality of additive tanks are prepared so that additives of a plurality of colors can be switched and supplied,
There is also an advantage that the color of the mixed reaction curable material can be easily changed. In any of the above embodiments, the third route of supplying from a route different from the respective routes of the main agent and the curing agent.
Although the internal mold release agent and the colorant were selected as the main component additives as the supply component of the above, one of the internal mold release agent and the colorant may be used as the third supply component, and further the internal mold release agent may be used. And an additive other than the colorant may be used as the third feed component. Further, in the embodiment, the supply method when the mixed reaction curable material is used for skin molding has been described, but the present invention is not limited to this, and the mixed reaction curable material is used for molding such as paint and injection molding. It can also be applied to the supply method in the case of doing.

【発明の効果】以上の説明から明らかなように、本発明
によれば、混合反応硬化型材料の主剤を気泡の噛み込み
を低減して混合室に供給でき、主剤と硬化剤との混合物
を気泡の噛み込みによる悪影響がない状態で使用に供す
ることができる。また材料の色の管理が容易になり、色
を変更する場合も、短時間で簡単に変更することができ
る。
As is apparent from the above description, according to the present invention, the main agent of the mixed reaction-curable material can be supplied to the mixing chamber while reducing the trapping of bubbles, and the mixture of the main agent and the curing agent can be obtained. It can be used without being adversely affected by the entrapment of bubbles. Further, the color of the material can be easily managed, and the color can be easily changed in a short time.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施の形態の供給方法を適用した混
合反応硬化型材料の供給ラインを示す説明図である。
FIG. 1 is an explanatory diagram showing a supply line of a mixed reaction curable material to which a supply method according to an embodiment of the present invention is applied.

【図2】本発明の他の実施の形態の供給方法を適用した
混合反応硬化型材料の供給ラインを示す説明図である。
FIG. 2 is an explanatory diagram showing a supply line for a mixed reaction curable material to which a supply method according to another embodiment of the present invention is applied.

【符号の説明】[Explanation of symbols]

10 主剤タンク 11、21 攪拌機 13、23 計量ポンプ 14、24 熱交換器 15、25 流量計 17、27 温調用熱媒ヒーター 18、28 開閉バルブ 20 硬化剤タンク 30 添加剤タンク 31 定量ポンプ 32 カラーチェンジャー 33 洗浄液タンク L1a 主剤供給ライン L1b 主剤戻りライン L2a 硬化剤供給ライン L2b 硬化剤戻りライン L3 添加剤供給ライン 10 Main agent tank 11, 21 stirrer 13, 23 metering pump 14, 24 heat exchanger 15, 25 Flowmeter 17, 27 Heat medium heater for temperature control 18, 28 open / close valve 20 Hardener tank 30 additive tank 31 metering pump 32 color changer 33 Cleaning liquid tank L1a Main agent supply line L1b Main agent return line L2a curing agent supply line L2b Hardener return line L3 additive supply line

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4F033 QA01 QB03X QB18 QD02 QD14 4F201 AA36 AB03 AB12 BA01 BC33 BK62 BK64 BN50 BQ02 BQ09 BQ20 BQ34 BQ40 BQ45 BQ50 BQ52 4G035 AB41 AE13 4G037 AA02 EA01    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4F033 QA01 QB03X QB18 QD02                       QD14                 4F201 AA36 AB03 AB12 BA01 BC33                       BK62 BK64 BN50 BQ02 BQ09                       BQ20 BQ34 BQ40 BQ45 BQ50                       BQ52                 4G035 AB41 AE13                 4G037 AA02 EA01

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 混合反応硬化型材料の主剤と硬化剤と
を、それぞれの供給経路から混合室に供給する混合反応
硬化型材料の供給方法において、 前記主剤の添加剤のうちの内部離型剤を主剤に配合せず
に第3の供給成分として、前記主剤および硬化剤の供給
経路とは別の供給経路から前記混合室に供給することを
特徴とする混合反応硬化型材料の供給方法。
1. A method for supplying a mixed reaction-curable material, wherein a main agent and a curing agent for the mixed reaction-curable material are supplied from respective supply paths to a mixing chamber, wherein an internal release agent of the additives for the main agent is used. A method for supplying a mixed reaction curable material, characterized in that, as a third supply component, is not mixed with the main agent and is supplied to the mixing chamber from a supply path different from the supply paths of the main agent and the curing agent.
【請求項2】 前記内部離型剤を主剤を用いて希釈し
たことを特徴とする請求項1記載の供給方法。
2. The supply method according to claim 1, wherein the internal release agent is diluted with a main agent.
【請求項3】 前記主剤の添加剤のうちの着色剤を更
に第3の供給成分として、前記内部離型剤に加えたこと
を特徴とする請求項1または2記載の供給方法。
3. The supply method according to claim 1, wherein a colorant among the additives of the main component is further added to the internal mold release agent as a third supply component.
JP2001374461A 2001-12-07 2001-12-07 Method for supplying mixing reaction curable material Pending JP2003170422A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001374461A JP2003170422A (en) 2001-12-07 2001-12-07 Method for supplying mixing reaction curable material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001374461A JP2003170422A (en) 2001-12-07 2001-12-07 Method for supplying mixing reaction curable material

Publications (1)

Publication Number Publication Date
JP2003170422A true JP2003170422A (en) 2003-06-17

Family

ID=19183017

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001374461A Pending JP2003170422A (en) 2001-12-07 2001-12-07 Method for supplying mixing reaction curable material

Country Status (1)

Country Link
JP (1) JP2003170422A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6047256B1 (en) * 2016-06-28 2016-12-21 大日本塗料株式会社 How to paint the road
CN111531146A (en) * 2020-05-14 2020-08-14 夏三头 Aluminum alloy die-casting release agent and preparation system and method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6047256B1 (en) * 2016-06-28 2016-12-21 大日本塗料株式会社 How to paint the road
CN111531146A (en) * 2020-05-14 2020-08-14 夏三头 Aluminum alloy die-casting release agent and preparation system and method thereof
CN111531146B (en) * 2020-05-14 2021-06-29 深圳市协力达精密科技有限公司 Aluminum alloy die-casting release agent and preparation system and method thereof

Similar Documents

Publication Publication Date Title
JP7270333B2 (en) Cleaning liquid for ink ejection head, set of ink and cleaning liquid for ink ejection head, cleaning method, cleaning apparatus, recording method, and recording apparatus
WO2018079513A1 (en) Cleaning solution, set of ink and cleaning solution, cleaning method, cleaning apparatus, printing method, and printing apparatus
HRP20110507T1 (en) Method for dyeing or bleaching the hair
CN101410470A (en) Process for producing aqueous pigment dispersion and ink for ink-jet recording
CN100430447C (en) Ink, ink for ink-jet printer, method for reducing scorching on surface of heater for ink-jet recording heat, ink-jet recording method and device, recorder
CN101218103A (en) Thermal inkjet ink and ink cartridge using the same
JP2003170422A (en) Method for supplying mixing reaction curable material
MXPA02010700A (en) Improved dosing assembly.
JP6443163B2 (en) Cleaning liquid, cleaning liquid and ink set kit, ink jet recording apparatus, and ink tank cleaning method
JPH10110127A (en) Recording solution for ink-jet
KR101377013B1 (en) Device for mixing multi-liquid paints of apparatus for painting traffic lane
JPH06226154A (en) Coating apparatus
JPH11128785A (en) Coating device and method for coating multi-color pattern
JP2005246167A (en) Multi-liquid mixing apparatus
JP3883861B2 (en) Method for supplying colored liquid used for reaction curable material
CN110167759A (en) For printing the method for different materials type of container in directly printing technique and directly printing machine
JP2018069723A (en) Cleaning liquid, set of ink and cleaning liquid, cleaning method, cleaning device, printing method, and printing device
US10752221B2 (en) Multicolor car wash station and process
JP2004154643A (en) Multi-liquid mixing apparatus, and multi-liquid mixing method
JP2003191232A (en) Liquid blending equipment
JP2017160404A (en) Cleaning fluid, set of ink and cleaning fluid, cleaning method, inkjet recording device and inkjet recording method
JP4882325B2 (en) Ink supply path cleaning method and cleaning apparatus
CN112644014A (en) 3D printer
JP2009254982A (en) Feed rate setting method of two liquid paint feeding device
JP2020200438A (en) Ink and printing method