JPS6130633B2 - - Google Patents
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- Publication number
- JPS6130633B2 JPS6130633B2 JP10067580A JP10067580A JPS6130633B2 JP S6130633 B2 JPS6130633 B2 JP S6130633B2 JP 10067580 A JP10067580 A JP 10067580A JP 10067580 A JP10067580 A JP 10067580A JP S6130633 B2 JPS6130633 B2 JP S6130633B2
- Authority
- JP
- Japan
- Prior art keywords
- agent
- curing agent
- paint
- curing
- base
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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- Application Of Or Painting With Fluid Materials (AREA)
- Nozzles (AREA)
Description
【発明の詳細な説明】 本発明は塗装方法の改良に関するものである。[Detailed description of the invention] The present invention relates to improvements in coating methods.
塗装工程の省エネルギー化、公害対策として塗
料乾燥工程の低温短時間化、塗料のハイソリツド
化が考えられているが、この要求に対して現在一
般的に使用されている1液型塗料に比べ主剤と硬
化剤とよりなる2液型塗料は容易に上記要求に満
足できるものである。 In order to save energy in the painting process and prevent pollution, it is considered that the paint drying process can be carried out at a lower temperature and in a shorter time, and the paint can be made to have a higher solidity. A two-component paint comprising a curing agent can easily satisfy the above requirements.
ところが、上記2液型塗料は主剤と硬化剤とを
混合してからの可使用時間(ポツトライフ)が例
えば6時間程度と短かいため、混合された未使用
塗料は廃去しなければならず塗料の歩留りが悪い
という不具合があつた。 However, the pot life of the above two-component paint after mixing the base agent and curing agent is short, for example, about 6 hours, so the unused mixed paint must be disposed of. There was a problem that the yield was poor.
これを解決するために、スプレーガンの直前で
2液を混合するスタテイツクミキサーが考案され
ているが、このミキサーは狭い管路内に邪魔板を
多数設けて2液流に乱れを生じさせて混合するも
のであるが、構造が複雑で大型になり、塗料がつ
まりやすく、コストが高く、また塗装作業終了時
にはスタテイツクミキサーおよびスプレーガン内
を十分に洗浄しないと硬化剤により主剤が硬化し
てしまうため作業性も悪いという不具合があつ
た。本発明は上記不具合を解消するもので、少な
くとも主剤と硬化剤または硬化促進剤とからなる
塗料を用いる塗装方法において、主剤と硬化剤ま
たは硬化促進剤とを高速気流中にそれぞれ独立に
流出させて微粒化混合させながらほぼ直線的にノ
ズルに向つて移動させ、さらにこの微粒化混合体
をノズルから流体衝突分散器に向けて高速噴出さ
せて上記流体衝突分散器への衝突時に生ずる圧力
変化および流れの乱れと急激な方向変化により分
散した超微粒化混合体とし、この超微粒化混合体
を被塗装物に塗布することを特徴とする塗装方法
に係るものである。 To solve this problem, a static mixer has been devised that mixes the two liquids just before the spray gun, but this mixer has many baffles installed in the narrow pipe to create turbulence in the flow of the two liquids. However, the structure is complicated and large, the paint tends to clog, and the cost is high.Also, if the static mixer and spray gun are not thoroughly cleaned at the end of the painting process, the hardening agent will harden the main agent. There was a problem that the workability was poor because it was stored away. The present invention solves the above-mentioned problems, and is aimed at, in a coating method using a paint consisting of at least a base ingredient and a curing agent or a curing accelerator, by allowing the base ingredient and the curing agent or curing accelerator to flow out independently into high-speed airflow. The atomized mixture is moved almost linearly toward a nozzle while being atomized and mixed, and the atomized mixture is jetted out at high speed from the nozzle toward a fluid collision disperser to reduce the pressure change and flow that occur when it collides with the fluid collision disperser. This invention relates to a coating method characterized by forming an ultra-fine mixture dispersed by turbulence and rapid changes in direction, and applying this ultra-fine mixture to an object to be coated.
したがつて、主剤と硬化剤または硬化促進剤と
は微粒化され同時に混合されるので、作業性が良
く、またあらかじめ主剤と硬化剤または硬化促進
剤とを混合しないため、従来のように混合してし
まつた未使用塗料を廃却するということがなく、
コストが安くなり、さらに可使用時間の短かい低
温短時間硬化型の塗料を使用でき、これにより焼
付乾燥温度のいつそうの低下と短時間化とを果せ
るものである。また、主剤と硬化剤または硬化促
進剤とを高速気流中に流出するだけで確実に両剤
は混合微粒化でき、構成も簡単になるものであ
る。 Therefore, the base resin and the curing agent or curing accelerator are atomized and mixed at the same time, resulting in good workability.Also, since the base resin and the curing agent or curing accelerator are not mixed in advance, it is not possible to mix them as before. There is no need to dispose of unused paint,
It is possible to use a low-temperature, short-time curing type paint that is less expensive and has a shorter usable life, thereby making it possible to lower the baking drying temperature and shorten the time. Furthermore, simply by flowing the main agent and the curing agent or curing accelerator into a high-speed air stream, both agents can be reliably mixed and atomized, and the structure is simple.
以下、本発明の実施例について具体的に説明す
る。第1図に示す第1実施例において、微粒化混
合装置1は導入管2と円筒管3と分散角調整器4
と流体衝突分散器5とからなり、導入管2は左端
を図示しない高圧ガス(空気)供給源に接続さ
れ、右端に円筒管3を固着し、中間部に縮径部6
と小径部7と拡径部0とを設け、上記小径部7に
は第1第2供給管8,9の端部が開口している。
上記円筒管3の右端はノズル10を形成し、分散
角調整器4は円筒管3の右部外周に設けらた円筒
体で右端部を鋭角状11に形成されている。ま
た、流体衝突分散器5は円筒管3の内壁に植立さ
れた2本のステー12に支持され円筒管3の長手
方向中心軸上に位置し、分散角調整器4より右方
にまで延びたシヤフト13と、同シヤフト13の
右端に固着され外周を鋭角状に形成された円盤1
4とからなつている。 Examples of the present invention will be specifically described below. In the first embodiment shown in FIG.
The inlet pipe 2 has its left end connected to a high-pressure gas (air) supply source (not shown), a cylindrical pipe 3 fixed to its right end, and a reduced diameter part 6 in the middle.
A small diameter part 7 and an enlarged diameter part 0 are provided, and the ends of the first and second supply pipes 8 and 9 are opened in the small diameter part 7.
The right end of the cylindrical tube 3 forms a nozzle 10, and the dispersion angle adjuster 4 is a cylindrical body provided on the right outer periphery of the cylindrical tube 3, and the right end thereof is formed into an acute angle shape 11. Further, the fluid collision disperser 5 is supported by two stays 12 installed on the inner wall of the cylindrical tube 3, is located on the central axis in the longitudinal direction of the cylindrical tube 3, and extends to the right of the dispersion angle adjuster 4. a shaft 13, and a disk 1 fixed to the right end of the shaft 13 and having an acute-angled outer periphery.
It consists of 4.
第1供給管8は流量制御装置15を通つて色替
装置16に接続されている。この色替装置16に
はシンナー供給口17、2つの主剤供給口18,
19が設けらている。第1主剤供給口18は塗料
レギユレータ35を介して主剤溜22からポンプ
21を介して主剤溜22に戻る第1閉ループ20
に接続されている。この主剤溜22には2液型塗
料の赤色の主剤が溜められている。また第2主剤
供給口19は塗料レギユレータ36を介して主剤
溜25からポンプ24を介して主剤溜25に戻る
第2閉ループ23に接続され、同主剤溜25には
上記主剤溜22とは異なつた色(黄色)の主剤が
溜められている。 The first supply pipe 8 is connected to a color change device 16 through a flow control device 15 . This color changing device 16 includes a thinner supply port 17, two main agent supply ports 18,
19 is provided. The first base agent supply port 18 is connected to a first closed loop 20 which returns from the base agent reservoir 22 via the paint regulator 35 to the base agent reservoir 22 via the pump 21.
It is connected to the. The main agent reservoir 22 stores a red main agent of a two-component paint. Further, the second base agent supply port 19 is connected to a second closed loop 23 that returns from the base agent reservoir 25 to the base agent reservoir 25 via the pump 24 via the paint regulator 36, and the base agent reservoir 25 has a second base agent reservoir 25 different from the base agent reservoir 22. The main ingredient of color (yellow) is stored.
第2供給管9は流量制御装置15を通つて3方
弁26に接続され、同3方弁26の流入口はポン
プ27を介して硬化剤溜28に接続され、また上
記3方弁26の戻り口も上記硬化剤溜28に接続
され、硬化剤溜28,3方弁26、ポンプ27に
より第3閉ループ30は形成されている。そし
て、上記硬化剤溜28には2液型塗料の硬化剤が
溜られている。29は被塗装物である。 The second supply pipe 9 is connected to a three-way valve 26 through a flow rate control device 15, and the inlet of the three-way valve 26 is connected to a curing agent reservoir 28 via a pump 27. The return port is also connected to the curing agent reservoir 28, and a third closed loop 30 is formed by the curing agent reservoir 28, the three-way valve 26, and the pump 27. The curing agent reservoir 28 stores a curing agent for a two-component paint. 29 is an object to be painted.
上記構成により、被塗装物29を塗装するとき
には、まずポンプ21,24,27を駆動し、主
剤溜22,25とポンプ21,24と上記主剤溜
22,25とからなる第1,2閉ループ20,2
3内を主剤まそれぞれ循環し、また硬化剤溜28
とポンプ27と3方弁26と硬化剤溜28からな
る第3閉ループ30内は硬化剤は循環する。さら
に、図示しない高圧ガス源から導入管2に2〜6
Kl/cm2の圧力を有する空気を供給する。 With the above configuration, when painting the object 29, the pumps 21, 24, 27 are first driven, and the first and second closed loops 20, which are composed of the main agent reservoirs 22, 25, the pumps 21, 24, and the main agent reservoirs 22, 25, are driven. ,2
The main agent is circulated through the curing agent reservoir 28.
The curing agent circulates within a third closed loop 30 consisting of the pump 27, the three-way valve 26, and the curing agent reservoir 28. Furthermore, 2 to 6
Supply air with a pressure of Kl/cm 2 .
次に、被塗装物を赤色に塗装するとときは色替
装置16を操作して第1閉ループ20と流量制御
装置15とを連通させると、赤色の主剤はポンプ
21により主剤溜22から塗料レギユレータ3
5、色替装置16、流量制御装置15を通つて主
剤が第1供給管8に送られる。また、硬化剤は3
方弁26を操作することにより第3閉ループ30
から塗料レギユレータ36、流量制御装置15に
送られ同流量制御装置15により主剤の量に応じ
た量が第2供給管9へ送られる。 Next, when painting the object red, the color change device 16 is operated to connect the first closed loop 20 and the flow rate control device 15, and the red base agent is transferred from the base agent reservoir 22 to the paint regulator 3 by the pump 21.
5. The main agent is sent to the first supply pipe 8 through the color change device 16 and the flow rate control device 15. In addition, the curing agent is 3
The third closed loop 30 is opened by operating the direction valve 26.
The paint regulator 36 and the flow rate control device 15 send an amount corresponding to the amount of the main agent to the second supply pipe 9.
そして、第1、第2供給管8,9から主剤およ
び硬化剤がそれぞれ一定量小径部7を流れる高速
空気中へ流出する。すると、上記主剤および硬化
剤は高速空気中に微粒化混合されて円筒管3のノ
ズル10に向つてほぼ直線的に移動し、この微粒
化混合体は上記ノズル10から高速噴出して流体
衝突分散器5に衝突し、同時に混合体は圧縮さ
れ、四方に膨張分散し、微粒化混合がさらに促進
される。 Then, a fixed amount of the main agent and curing agent each flow out from the first and second supply pipes 8 and 9 into the high-speed air flowing through the small diameter portion 7. Then, the base agent and curing agent are atomized and mixed in high-speed air and moved almost linearly toward the nozzle 10 of the cylindrical tube 3, and this atomized mixture is jetted out at high speed from the nozzle 10 and is dispersed by fluid collision. The mixture collides with the vessel 5, and at the same time is compressed, expands and disperses in all directions, and further promotes atomization and mixing.
この膨張分散した微粒化混合体にノズル10か
ら噴出した後続の微粒化混合体が衝突し、分散角
調整器4の鋭角11と流体衝突分散器5の鋭角状
の円周とにより抱束されて外部へ急速分散し、こ
れによりさらに主剤と硬化剤の微粒化と混合とが
進み、この超微粒化混合体は被塗装物に付着す
る。そして、硬化剤の作用により主剤は硬化す
る。 The subsequent atomized mixture ejected from the nozzle 10 collides with this expanded and dispersed atomized mixture, and is bound by the acute angle 11 of the dispersion angle adjuster 4 and the acute angle circumference of the fluid collision disperser 5. It is rapidly dispersed to the outside, which further advances the atomization and mixing of the base agent and curing agent, and this ultra-atomized mixture adheres to the object to be coated. Then, the main ingredient is cured by the action of the curing agent.
また、黄色を塗布するときには色替装置16を
操作して、第1閉ループ20への連通を遮断し、
シンナー供給口17を開いてシンナーを同供給口
17から流量制御装置15、第1供給管8を通つ
て微粒化混合装置1内に流出し、高速空気流によ
り外部へ噴出される。このとき、色替装置16、
流量制御装置15、第1供給管8、それらを結ぶ
管路および微粒化混合装置1内に付着した赤色の
主剤を洗い流す。次に、色替装置16を操作し
て、第2閉ループ23を色替装置16へ連通し、
黄色の主剤を主剤溜25から色替装置16、流量
制御装置15、第1供給管8、微粒化混合装置1
へ流し、同混合装置1で硬化剤と微粒化混合され
て被塗装物へ塗布する。 Also, when applying yellow, operate the color change device 16 to cut off communication to the first closed loop 20,
The thinner supply port 17 is opened, and the thinner flows from the supply port 17 into the atomization mixing device 1 through the flow rate control device 15 and the first supply pipe 8, and is ejected to the outside by a high-speed air flow. At this time, the color changing device 16,
The red base agent adhering to the flow rate control device 15, the first supply pipe 8, the pipe line connecting them, and the inside of the atomization mixing device 1 is washed away. Next, operate the color change device 16 to connect the second closed loop 23 to the color change device 16,
The yellow main agent is transferred from the main agent reservoir 25 to the color changing device 16, the flow rate control device 15, the first supply pipe 8, and the atomization mixing device 1.
The mixture is mixed with a curing agent into fine particles in the same mixing device 1, and then applied to the object to be coated.
したがつて、主剤と硬化剤とからなる2液型塗
料を用いるため、焼付乾燥工程における温度の低
下、時間短縮が計れ、エネルギーの節約と低コス
ト化および作業能率の向上が得られるものであ
る。 Therefore, since a two-component paint consisting of a base agent and a curing agent is used, it is possible to lower the temperature and shorten the time during the baking drying process, resulting in energy savings, lower costs, and improved work efficiency. .
また、主剤と硬化剤とを微粒化混合装置1内で
混合させるため、従来のようにあらかじめ2液を
混合させておくもののように塗装作業終了時(装
置の運転終了時)に余つた塗料を廃却するという
必要がなく、塗料の歩留りがよい。 In addition, since the main agent and curing agent are mixed in the atomization mixing device 1, it is possible to use the remaining paint at the end of the painting work (when the device is finished operating), unlike the conventional method in which the two liquids are mixed in advance. There is no need to dispose of it, and the yield of paint is good.
さらに、微粒化混合装置1は従来のスタテイツ
クミキサーに比べ構造が簡単で、コストが安く、
しかも目づまりを起すことがなく、十分な混合と
微粒化とを計れるものである。 Furthermore, the atomization mixing device 1 has a simpler structure and lower cost than conventional static mixers.
Furthermore, sufficient mixing and atomization can be achieved without causing clogging.
また、主剤と硬化剤の混合が微粒化混合装置1
内で行なわれるので、混合塗料の可使用時間を極
めて短かくでき、これにより極めて低温短時間で
硬化する塗料を用いることができる。 In addition, the mixing of the base agent and the curing agent is carried out in the atomization mixing device 1.
Since the process is carried out within a room, the usable life of the mixed paint can be extremely shortened, and as a result, a paint that cures at extremely low temperatures and in a short time can be used.
なお、上記実施例において第1第2供給管8,
9を小径部7に開口したが拡径部0に設けてもよ
いものである。 In addition, in the above embodiment, the first and second supply pipes 8,
9 is opened in the small diameter part 7, but it may be provided in the enlarged diameter part 0.
また、上記実施例において微粒化混合装置1に
は第1第2供給管8,9により主剤と硬化剤とを
供給しているが、第3供給管を設けてここからシ
ンナーを供給して塗料を希釈することもできる。
また、上記第3供給管から硬化促進剤(SN等)
を供給して硬化を促進させることもできる。 Further, in the above embodiment, the main agent and curing agent are supplied to the atomization mixing device 1 through the first and second supply pipes 8 and 9, but a third supply pipe is provided from which thinner is supplied and the paint is It can also be diluted.
In addition, a curing accelerator (S N , etc.) is supplied from the third supply pipe.
can also be supplied to accelerate curing.
さらに、上記実施例の微粒化混合装置1に4個
以上の供給管を開口せしめて4液以上の塗料、添
加物を供給することができることももちろんであ
る。なお、上記実施例において使用する主剤と硬
化剤とからなる2液性塗料には例えば、ウレタン
樹脂脂塗料、ポリエステル樹脂塗料、エポキシ樹
脂塗料、酸硬化型アミノアルキド樹脂塗料等があ
る。 Furthermore, it goes without saying that four or more supply pipes can be opened in the atomization mixing device 1 of the above embodiment to supply four or more liquids of paint and additives. The two-component paint consisting of a main agent and a curing agent used in the above examples includes, for example, a urethane resin paint, a polyester resin paint, an epoxy resin paint, an acid-curable aminoalkyd resin paint, and the like.
また、硬化促進剤である酸触媒を第2供給管か
ら供給し、メラミン−アルキドあるいはアクリル
−メラミン樹脂塗料等を第1供給管から供給させ
る2液もしくはそれ以上の多液型塗料を用いても
よいものである。 It is also possible to use a two-component or more multi-component paint in which the acid catalyst, which is a curing accelerator, is supplied from the second supply pipe and the melamine-alkyd or acrylic-melamine resin paint is supplied from the first supply pipe. It's good.
第2図に示す第2実施例におて第1実施例と共
通するものについては同一符号を付して説明す
る。第2図において、第1閉ループ20は主剤溜
22とギヤポンプ31の第1ポンプ部32と3方
弁33とからなり、3方弁33の吐出側は微粒化
混合装置1の第1供給管8に接続されている。第
3閉ループ30は硬化剤溜28とギヤポンプ31
の第2ポンプ部34と3方弁26とから形成され
ている。上記ギヤポンプ部31は第1第2ポンプ
部32,34において常に一定量の主剤および硬
化剤を吐出させる。 Components in the second embodiment shown in FIG. 2 that are common to the first embodiment will be described with the same reference numerals. In FIG. 2, the first closed loop 20 consists of a main agent reservoir 22, a first pump section 32 of a gear pump 31, and a three-way valve 33, and the discharge side of the three-way valve 33 is connected to the first supply pipe 8 of the atomization mixing device 1. It is connected to the. The third closed loop 30 includes a curing agent reservoir 28 and a gear pump 31.
It is formed from a second pump section 34 and a three-way valve 26. The gear pump section 31 causes the first and second pump sections 32 and 34 to always discharge a constant amount of the main agent and curing agent.
したがつて、塗装を行なうときには、まずギヤ
ポンプ31を駆動させて第1第3閉ループ20,
30内に主剤および硬化剤を循環させる。次に3
方弁26,33を操作して第1第3閉ループ2
0,30内での循環を止め第1第2供給管8,9
の方に流れるようにし、主剤を第1供給管8から
微粒化混合装置1内を流れる高速気流中に、また
硬化剤も第2供給管9から微粒化混合装置1内を
流れる高速気流中にそれぞれ流出させて、微粒化
混合分散を行ない、この微粒化混合分散体を被塗
装物に塗布する。 Therefore, when painting, the gear pump 31 is first driven and the first and third closed loops 20,
The main agent and curing agent are circulated within the container 30. Next 3
The first and third closed loops 2 are operated by operating the direction valves 26 and 33.
Stop the circulation within the first and second supply pipes 8 and 9.
so that the base agent flows from the first supply pipe 8 into the high-speed airflow flowing through the atomization mixing device 1, and the curing agent also flows from the second supply pipe 9 into the high-speed airflow flowing through the atomization mixing device 1. Each of them is flowed out, atomized and mixed and dispersed, and this atomized mixed and dispersion is applied to an object to be coated.
よつて、1つのギヤポンプ31で主剤と硬化剤
とをそれぞれ定量づつ吐出するので、ポンプの数
を低減でき、さらに流量制御装置を設けなくとも
よいため塗装設備のコストが安くなるものであ
る。 Therefore, since one gear pump 31 discharges the main agent and the curing agent in fixed amounts, the number of pumps can be reduced, and there is no need to provide a flow rate control device, so the cost of the coating equipment can be reduced.
第1図は本発明の第1実施例を示す説明図、第
2図は本発明の第2実施例を示す説明図である。
1:微粒化混合装置、4:分散角調整器、5:
流体衝突分散器、8,9:供給管、15:流量制
御装置、16:色替装置、21,24,27:ポ
ンプ、22,25:主剤溜、28:硬化剤溜、2
0,23,30:閉ループ、31:ギヤポンプ。
FIG. 1 is an explanatory diagram showing a first embodiment of the invention, and FIG. 2 is an explanatory diagram showing a second embodiment of the invention. 1: Atomization mixing device, 4: Dispersion angle adjuster, 5:
Fluid collision disperser, 8, 9: Supply pipe, 15: Flow rate control device, 16: Color change device, 21, 24, 27: Pump, 22, 25: Main agent reservoir, 28: Hardening agent reservoir, 2
0, 23, 30: closed loop, 31: gear pump.
Claims (1)
からなる塗料を用いる塗装方法において、主剤と
硬化剤または硬化促進剤とを高速気流中にそれぞ
れ独立に流出させて微粒化混合させながらほぼ直
線的にノズルに向つて移動させ、さらにこの微粒
化混合体をノズルから流体衝突分散器に向けて高
速噴出させて上記流体衝突分散器への衝突時に生
ずる圧力変化および流れの乱れと急激な方向変化
により分散した超微粒化混合体とし、この超微粒
化混合体を被塗装物を塗布することを特徴とする
塗装方法。1. In a coating method using a paint consisting of at least a base agent and a curing agent or a curing accelerator, the base agent and the curing agent or curing accelerator are flowed out independently into a high-speed air stream, and mixed into atomized particles almost linearly through a nozzle. This atomized mixture was then ejected at high speed from a nozzle toward a fluid collision disperser, and was dispersed by the pressure change, flow turbulence, and sudden direction change that occurred when it collided with the fluid collision disperser. A coating method characterized by forming an ultra-fine particle mixture and applying this ultra-fine particle mixture to an object to be coated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10067580A JPS5724671A (en) | 1980-07-22 | 1980-07-22 | Coating method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10067580A JPS5724671A (en) | 1980-07-22 | 1980-07-22 | Coating method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5724671A JPS5724671A (en) | 1982-02-09 |
| JPS6130633B2 true JPS6130633B2 (en) | 1986-07-15 |
Family
ID=14280326
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10067580A Granted JPS5724671A (en) | 1980-07-22 | 1980-07-22 | Coating method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5724671A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61101274A (en) * | 1984-10-22 | 1986-05-20 | Trinity Ind Corp | Painting method |
-
1980
- 1980-07-22 JP JP10067580A patent/JPS5724671A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5724671A (en) | 1982-02-09 |
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