JPS59213468A - Painting method of reaction curing type - Google Patents

Painting method of reaction curing type

Info

Publication number
JPS59213468A
JPS59213468A JP8539883A JP8539883A JPS59213468A JP S59213468 A JPS59213468 A JP S59213468A JP 8539883 A JP8539883 A JP 8539883A JP 8539883 A JP8539883 A JP 8539883A JP S59213468 A JPS59213468 A JP S59213468A
Authority
JP
Japan
Prior art keywords
agent
valve
curing
supplied
additive
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.)
Granted
Application number
JP8539883A
Other languages
Japanese (ja)
Other versions
JPH0318502B2 (en
Inventor
Tatsuo Fuchimoto
渕本 辰男
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.)
NIPPON RANZUBAAGU KK
Carlisle Fluid Technologies Ransburg Japan KK
Original Assignee
NIPPON RANZUBAAGU KK
Ransburg Japan 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 NIPPON RANZUBAAGU KK, Ransburg Japan Ltd filed Critical NIPPON RANZUBAAGU KK
Priority to JP8539883A priority Critical patent/JPS59213468A/en
Publication of JPS59213468A publication Critical patent/JPS59213468A/en
Publication of JPH0318502B2 publication Critical patent/JPH0318502B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To mix a base material and a hardener always at a highly accurate mixing ratio by detecting the respective amt. of the base material and hardener supplied, comparing the supply ratios with a set mixing ratio and controlling the mixing ratio. CONSTITUTION:The respective amts. of the base material and hardener supplied from base material supplying lines 12-17, 47 and hardener supplying lines 31, 32, 48 are detected with detectors 56-60. The detected amts. and a preset mixing ratio are compared and the amts. of the base material and hardener to be supplied are controlled to attain the preset mixing ratio. Then the always highly accurate mixing ratio is assured even if the amts. of said materials to be supplied fluctuate and the environmental conditions change.

Description

【発明の詳細な説明】 本発りjは2液性反応硬化型塗料ま/ζは3液性反応硬
化型塗料を用いて塗装作業を行なうための反応硬化型塗
料の塗装方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for applying a reaction-curing paint for performing painting work using a two-component reaction-curing paint or a three-component reaction-curing paint. .

一般に、ポリウレタン樹脂塗料、不飽和ポリエステル樹
脂塗料、工、IPキシ樹脂塗料等の反応硬化型塗料に1
、溶剤分が少なく、塗膜の硬化乾燥の際に熱エネルギを
必要としない′帛篇反応硬化が可能なことから注目され
てきている。
Generally, 1 is used for reaction-curing paints such as polyurethane resin paints, unsaturated polyester resin paints, polyurethane resin paints, and IP xy resin paints.
It has been attracting attention because it contains a small amount of solvent and is capable of curing by a 'textile reaction', which does not require thermal energy during curing and drying of the coating film.

しかし、この反応硬化型塗料Cポットライフ(可使用時
間)の問題から調合ないしは混合状態での製造、流通は
不可能であシ、主剤と硬化剤の2成分、または主剤と硬
化剤と添加剤の3成分から構成し、しかもこれらを別個
の容器および供給系統として取扱い、塗装置前に混合し
た後噴霧しなくてはならないという問題虞がある。また
、主剤の種類、主剤中に含1れる顔料の種類等に応じて
、当該主剤と硬化剤との混合圧出、または主剤と硬化剤
と添加剤との混合死出を高精度に管理しなくてはならな
いという問題点がある。
However, due to problems with the pot life (pot life) of this reaction-curing paint, it is impossible to manufacture or distribute it in a blended or mixed state. However, there is a problem in that these three components must be handled as separate containers and supply systems, and must be mixed and then sprayed before application. In addition, depending on the type of base resin, the type of pigment contained in the base resin, etc., the mixture extrusion of the base resin and curing agent, or the mixture extrusion of the base resin, curing agent, and additives can be controlled with high precision. There is a problem that it is indispensable.

このため、従来方式によるものは主剤供給系統と硬化剤
供給系統とからそれぞれ供給される主剤と硬化剤とを混
合することによって混合体となし、この混合体を塗装機
から被塗物に向けて噴霧するに際し、主剤供給系統と硬
化剤供給系統の途中に一対のポンプからなる2液定比率
ボンfまたは一対の削岳シリンダ装局を挿入し、これら
ポンプの吐出容積比または各!llクシリンダ装置間ス
トローク比を変更することによって混合圧出を管理する
ようにしたものが知られている。
For this reason, in the conventional method, a mixture is created by mixing the main agent and curing agent supplied from the main agent supply system and the curing agent supply system, respectively, and this mixture is directed from the coating machine to the object to be coated. When spraying, a two-liquid fixed-ratio bomb consisting of a pair of pumps or a pair of drilling cylinder units is inserted between the main agent supply system and the curing agent supply system, and the discharge volume ratio of these pumps or each! A device is known in which mixed pressure is managed by changing the stroke ratio between cylinder devices.

しかし、上記従来方法によるものは混合死出を変更する
毎に2液定比ホ?ンゾの回転比または計最シリンダ装置
のストローク比を機械的に変更しなくではならず、その
操作が非常に煩わしいという欠点があった。また、上記
従来方法によるものはシーケンス的な制御であるため、
混合比率を正確に行なっても温度、粘度等の外囲条件に
よる供給量の変動を常時監視することができないという
欠点があった。さらに、主剤の種類や塗色の種類を変更
し、または色替しつつ多種類の塗料を連続的に噴霧する
ようなシステムとして構成することができず、かつ添加
剤については別途混合死出の管理を行なわなくてはなら
ないという欠点があった0 本発明は前述の各欠点に鑑みなされたもので、塗装置前
での混合を可能とすると共に、主剤と硬化剤、または主
剤と硬化剤と添加剤の供給」λをそれぞれ検出し、当該
検出量に基づいて高精度な混合死出を維持しうるように
した反応硬化へす塗料の塗装方法を提供することを目的
とするものである。
However, in the conventional method described above, each time the mixing ratio is changed, the two-liquid constant ratio is changed. However, it is necessary to mechanically change the rotation ratio of the engine or the stroke ratio of the total cylinder device, which has the disadvantage that the operation is very troublesome. In addition, since the conventional method described above is sequential control,
Even if the mixing ratio is adjusted accurately, there is a drawback in that it is not possible to constantly monitor fluctuations in the supply amount due to ambient conditions such as temperature and viscosity. Furthermore, it is not possible to configure a system that continuously sprays many types of paint while changing the type of base agent or color, and additives must be mixed separately. The present invention was developed in view of the above-mentioned drawbacks, and it enables mixing of the base material and curing agent, or the base material and curing agent, before painting. It is an object of the present invention to provide a method for coating a reaction-curing paint, which detects the additive supply λ and maintains highly accurate mixing based on the detected amount.

上記目的を達成するために、この出願に係る第1の発明
が採用する構成の特徴は、主剤供給系統と硬化剤供給系
統からそれぞれ供給されている供給量を検出し、当該主
剤と硬化剤の供給死出と予め設定された混合圧出とを比
較し、前記主剤と硬化剤の供給量を予め設定された混合
死出となるように制御するようにしたことにある。
In order to achieve the above object, the feature of the configuration adopted by the first invention of this application is to detect the supply amounts respectively supplied from the main agent supply system and the curing agent supply system, and to The present invention is characterized in that the supply amount and the preset mixing ratio are compared, and the supply amounts of the base resin and curing agent are controlled so as to achieve the preset mixing ratio.

捷た、この出願に係る第2の発明が採用する構成のキ1
.激は、主剤供給系統、硬化剤供給系統および添加剤供
給系統からそれぞれ供給されている供給量を検出し、当
該検出量と予め設定された混合圧出とを比較し、前記主
剤、硬化剤および添加剤の供給量を予め設定された混合
圧出となるように制御するようにしたことにある。
Key 1 of the configuration adopted by the second invention related to this application
.. The controller detects the supply amounts supplied from the main agent supply system, curing agent supply system, and additive supply system, and compares the detected amounts with a preset mixing extrusion, and calculates the amount of the main agent, curing agent, and The present invention is characterized in that the supply amount of the additive is controlled so as to achieve a preset mixing pressure.

以下、本発明について図面に示ず実施例に基づいて説明
する。
The present invention will be described below based on embodiments not shown in the drawings.

第1図は本発明の第1の実施例を示し、図中1は色替弁
装置を示し、該色替弁装r!t1は内部に主剤通路2人
を有するマニホールド2と、流出側が該主剤通路2Aに
接続されたエア弁3、シンナ弁4および複数の主剤弁5
,6.7とから大略構成され、前記エア弁3、シンナ弁
4としては例えばエア駆動式のスプリングリターン型2
ポート2位置切換弁が用いられ、また主剤弁5,6.7
としては例えばエア駆動式のスプリングリターン型3ポ
ート2位置切換弁が用いられる。そして、エア弁3、シ
ンナ弁4はマニホールド2の主剤通路2人最上流側に配
置され、エア弁3はエア配管8を介してエア源9と接続
され、シンナ弁4はシン−7[管10を介してシンナ源
としてのザーキュレーションパイプ11に接続され、こ
れらエア弁3、シンナ弁4は制御エアが供給されない限
り、常時は閉弁位置にある。一方、前記主剤弁5,6.
7は主剤配管12.13.14を介してA色、B色。
FIG. 1 shows a first embodiment of the present invention, in which numeral 1 indicates a color change valve device, and the color change valve device r! t1 includes a manifold 2 having two main agent passages therein, an air valve 3 whose outflow side is connected to the main agent passage 2A, a thinner valve 4, and a plurality of main agent valves 5.
, 6.7, and the air valve 3 and thinner valve 4 are, for example, an air-driven spring return type 2.
A port 2 position switching valve is used, and main agent valves 5, 6.7
For example, an air-driven spring return type three-port two-position switching valve is used. The air valve 3 and the thinner valve 4 are arranged on the most upstream side of the two main agent passages of the manifold 2, the air valve 3 is connected to the air source 9 via the air piping 8, and the thinner valve 4 is connected to the thinner valve 4 through the air pipe 8. The air valve 3 and the thinner valve 4 are normally in a closed position unless control air is supplied. On the other hand, the main agent valves 5, 6.
7 is color A and color B via main agent piping 12, 13, and 14.

0色の主剤タンク15,16.17にそれぞれ接続され
ると共に、戻シ配管18,19.20を介して前記各主
剤配管12,13.14と接続され、主剤配管12,1
3.14の途中にけ各戻シ配管18.19.20の接続
位桁と主剤弁5.6.7との間に例えば歯車ポンプ等の
容積型ポンプからなる主剤用ポンプ21,22.23が
設けられ、該各ポンプ21,22.23は主剤用モータ
24により駆動せしめられるように構成されている。
It is connected to the main agent tank 15, 16.17 of color 0, and also connected to each of the main agent piping 12, 13.14 via the return pipe 18, 19.20, and the main agent piping 12, 1
In the middle of 3.14, between the connection girder of each return pipe 18, 19, 20 and the main agent valve 5.6.7, the main agent pumps 21, 22, 23, which are positive displacement pumps such as gear pumps, are installed. are provided, and each of the pumps 21, 22, 23 is configured to be driven by a main agent motor 24.

そして、前記主剤弁5,6.7に制御エアが供給されな
い状態においては、主剤用ΣJ!′ンプ21,22゜2
3の駆動によって、該主剤用ポンプ21,22゜23、
主剤配管12,13,14、主剤弁5,6゜7、戻シ配
管18,19.20の間を循環している。
When control air is not supplied to the main agent valves 5, 6.7, the main agent ΣJ! 'Pump 21, 22゜2
3, the main agent pumps 21, 22, 23,
It circulates between the main agent pipes 12, 13, 14, the main agent valves 5, 6°7, and the return pipes 18, 19, 20.

25は硬化剤切換弁装置゛で、該硬化剤切換弁装置25
は内部に硬化剤通路26Aをイjするマニホールド26
と、流出側が該硬化剤通路26Aに接続されるシンナ弁
27、硬化剤弁28とから大略H1ス成され、シンナ弁
27はh1■述と同様のエア駆動式のスプリングリター
ン型2d?−)2位置切換弁が用いられ、また硬化剤弁
28もエア駆動式のノブリングリターン型3ポート2位
名゛切換弁が用いられる。そして、シンナ弁27はマニ
ホールド26の硬化剤通路26A上流側に配置され、該
らンナ弁27はシンナ配管29を介してシンナ源として
のザーキュレーションパイプ30に接続されている。一
方、硬化剤弁28は硬化剤配管31を介して硬化剤源3
2と接続されると共に、戻シ配管33を介して前記硬化
剤配管31と接続され、この硬化剤配管31の途中には
戻り配管33の接続位置と硬化剤弁28との間に例えば
歯車ポンプ等の容積型ポンプからなる硬化剤用d?ポン
プ4が設けられ、該ポンプ34は硬化剤用モータ35に
より F9X動せしめられるように構成されている。そ
して、前記シンナ弁27は制御エアが供給されない限シ
、常時は閉弁位置にあシ、一方硬化剤弁28は制御エア
が供給されない状態においては、硬化剤用ポンプ34の
駆動によって、該ポンプ34、硬化剤配管31、硬化剤
弁28、戻り配管33の間を循環している。
25 is a curing agent switching valve device, and the curing agent switching valve device 25
is a manifold 26 with a curing agent passage 26A inside.
The thinner valve 27 and the hardening agent valve 28, whose outflow side is connected to the hardening agent passage 26A, are approximately H1, and the thinner valve 27 is an air-driven spring return type 2d? similar to the one described in H1. -) A 2-position switching valve is used, and the curing agent valve 28 is also an air-driven knob ring return type 3-port 2-position switching valve. The thinner valve 27 is arranged upstream of the hardening agent passage 26A of the manifold 26, and the thinner valve 27 is connected to a circulation pipe 30 as a thinner source via a thinner pipe 29. On the other hand, the curing agent valve 28 is connected to the curing agent source 3 via the curing agent piping 31.
2 and the hardening agent pipe 31 via a return pipe 33, and a gear pump, for example, is connected to the hardening agent pipe 31 between the connection position of the return pipe 33 and the hardening agent valve 28. d? for curing agent consisting of a positive displacement pump such as A pump 4 is provided, and the pump 34 is configured to be driven by a curing agent motor 35. The thinner valve 27 is normally in the closed position unless control air is supplied, while the hardener valve 28 is operated by the hardener pump 34 when the control air is not supplied. 34, the hardening agent pipe 31, the hardening agent valve 28, and the return pipe 33.

36は添加剤切換弁装置で、該添加剤切換弁装@36は
内部に添加剤通路37Aを有するマニホールド37と、
流出側が該添加剤通路37Aに接続されるシンナ弁38
、添加剤弁39とから大略構成され、シンナ弁38は前
述と同様のエア駆動式のスプリングリターン型2ボート
2位置切換弁が用いられ、また添加剤弁39もエア駆動
式のスプリングリターン型3ポート2位買切換弁が用い
られる。そして、シンナ弁38はマニホールド37の添
加剤通路37A上流側に配置され、該シンナー弁38は
シンナ配管40を介してシンナ源としてのザーキュレー
ションパイプ41に接続すれている。一方、添加剤弁3
9は添加剤配管42を介して例えば溶剤、表面張力低下
剤、硬化遅延剤等の添加剤を貯える添加剤源43と接続
されると共に、戻り配管44を介して前記添加剤配管4
2と接続され、この添加剤配管42の途中には戻り配管
44の接続位置と添加剤弁39との間に前述と同様例え
ば歯車ポンプ等の客待型2ンプからなる添加剤用ボン7
’45が設けられ、該ポンプ45は添加剤用モータ46
によりi動ぜしめられるように構成されている。そして
、前記シンナ弁38は制御エアが供給され力い限シ、常
時は閉弁位置にあり、一方硬化剤弁39は制御エアが供
給されない状態においては、添加剤用ポンプ45の駆動
によって、該ポンプ45、添加剤配管42、添加剤弁3
9、戻シ配管44の間を循環している。
36 is an additive switching valve device, and the additive switching valve device @36 includes a manifold 37 having an additive passage 37A therein;
Thinner valve 38 whose outflow side is connected to the additive passage 37A
, an additive valve 39, and the thinner valve 38 is an air-driven spring return type 2-boat 2-position switching valve similar to that described above, and the additive valve 39 is also an air-driven spring return type 3 valve. A port 2-position switching valve is used. The thinner valve 38 is arranged upstream of the additive passage 37A of the manifold 37, and the thinner valve 38 is connected to a circulation pipe 41 as a thinner source via a thinner pipe 40. On the other hand, additive valve 3
9 is connected via an additive pipe 42 to an additive source 43 storing additives such as a solvent, a surface tension reducing agent, a curing retarder, etc., and is connected to the additive pipe 4 via a return pipe 44.
2, and in the middle of this additive pipe 42, between the connecting position of the return pipe 44 and the additive valve 39, there is an additive cylinder 7, which is a customer-ready type 2 pump such as a gear pump, as described above.
'45 is provided, and the pump 45 is connected to an additive motor 46.
It is configured such that it can be moved by i. The thinner valve 38 is normally in the closed position as long as control air is supplied, while the hardener valve 39 is in the closed position as long as the control air is not supplied. Pump 45, additive piping 42, additive valve 3
9 and the return pipe 44.

47.48.49はそれぞれ主剤配管、硬化剤配管、添
加剤配管を示し、該各氏管47.48゜49の一端は各
マニホールド2,26.37の流出口と接続され、その
他端は例えばスタテツクミキザのようなラインミキサ5
0と接続され、かつ該各氏v47.48.49の途中に
0]各マニホールド2.26.37からラインミキサ5
0に向けてのみ液体の流通を許す逆止弁51,52.5
3がそれぞれ設けられている。54は一端がラインミキ
サ50の流出側に接続された塗料パイプで、該塗料パイ
プ54の他端には例えばエアガン、エアレスガン等から
なる塗装機55が設けられ、該塗装機55は必要に応じ
て高電圧が印加されて静電塗装機を構成している。
Reference numerals 47, 48, and 49 indicate main agent piping, curing agent piping, and additive piping, respectively. One end of each pipe 47.48° 49 is connected to the outlet of each manifold 2, 26.37, and the other end is connected to a static mixer, for example. Line mixer 5 like
0 and in the middle of each manifold 2.26.37 to line mixer 5
Check valves 51, 52.5 that allow liquid to flow only towards zero
3 are provided respectively. 54 is a paint pipe whose one end is connected to the outflow side of the line mixer 50, and the other end of the paint pipe 54 is provided with a coating machine 55 consisting of, for example, an air gun, an airless gun, etc., and the coating machine 55 can be used as needed. A high voltage is applied to constitute an electrostatic coating machine.

一方、56.57,58,59.60は各パ?ンプ21
,22,23.34.45に取付けられた回転検出器で
、該各回転検出器56〜60は訪各sDンプ21〜23
.34,35の回転数を検出すう)を出力するようにな
されている。なお、前記各yJ?ンプ21〜23,34
.35として容積榎ポンプを使用することによシ、これ
らの回転数に所定の流量係数をJJllけることにより
実流mとして計量することができるから、供給量信号を
デジタルまたはアナログ的に引数することによって供給
量を知ることができる。
On the other hand, 56.57, 58, 59.60 are each par? pump 21
, 22, 23, 34, and 45, and each of the rotation detectors 56 to 60 is connected to each sD pump 21 to 23.
.. 34 and 35) is output. In addition, each of the above yJ? 21-23, 34
.. By using a positive displacement pump as 35, it is possible to measure the actual flow m by subtracting a predetermined flow coefficient to these rotational speeds, so the supply amount signal can be expressed digitally or analogously. The amount of supply can be determined by

さらに、61は例えばノ・−ド回路、マイクロコンピュ
ータ等からなるflilJ彷j装置、62は主剤、硬化
剤および添加剤の混合比率を各主剤の秤類に応じて所望
の比率に自動的に設定する混合比率設定器を示し、前記
制御装置61は混合比率設定器62で予め設定され、入
力された所定の混合比率と、信号線63〜67を介して
入力される回転検出i:’:56〜60からの供給量信
号とを比較し、この比較結果に基づいてモータ24,3
5.46の回転数を混合比率設定器62で予め設定した
混合比どことなるように制御する機能を有する。従って
前記制御装置61からは、信号線68 、69.70ヲ
介シてモータ24.35.46に回転制御信号を出力し
、該各モータ24,35.4Gをそれぞれ所定の回転数
で回転せしめ、これによυポンプ21〜23,34.4
5を所定の混合比率となるように回転駆動せしめる。
Furthermore, reference numeral 61 is a fliljergy device comprising, for example, a node circuit, a microcomputer, etc., and 62 is a device that automatically sets the mixing ratio of the base resin, curing agent, and additives to a desired ratio according to the scale of each base resin. The control device 61 uses a predetermined mixture ratio that is preset and inputted by a mixing ratio setting device 62 and a rotation detection i:':56 that is inputted via signal lines 63 to 67. - 60, and based on this comparison result, the motors 24, 3
It has a function of controlling the rotation speed of 5.46 to a mixing ratio preset by a mixing ratio setting device 62. Therefore, the control device 61 outputs a rotation control signal to the motors 24, 35, 46 through the signal lines 68, 69, 70, and causes each motor 24, 35.4G to rotate at a predetermined number of rotations. , this causes υ pumps 21 to 23, 34.4
5 is rotated to achieve a predetermined mixing ratio.

本実施例に用いる塗装装置は以上のように構成されるが
、次にこの塗装装置を用いた塗装方法について述べる。
The coating apparatus used in this embodiment is constructed as described above. Next, a coating method using this coating apparatus will be described.

いま、前述の装置を構成する要素は全て清浄に洗浄され
ているものとする。この状態で、主剤源15に貯えられ
ているA色の主剤を用いて塗装作業を行なうものとする
It is now assumed that all the elements constituting the above-mentioned apparatus have been thoroughly cleaned. In this state, it is assumed that a painting operation is performed using the base material of color A stored in the base material source 15.

このA色の主剤に対して、該主剤と硬化剤と添加剤との
混合比率が10:2:1であると仮定すると、塗装作業
の開始操作によってこれを混合比率設定器62で設定さ
れた値を自動的に制御装置61に入力し、その記憶領域
に記憶せしめる。々お、この設定操作は手動設定であっ
てもよい。
Assuming that the mixing ratio of the main material, curing agent, and additive for this color A main material is 10:2:1, this is set by the mixing ratio setting device 62 in the starting operation of the painting operation. The value is automatically input into the control device 61 and stored in its storage area. Alternatively, this setting operation may be a manual setting.

次に、主剤弁5、硬化剤弁28、添加剤弁39に制御エ
アを供給して弁切換を行ない、信号線68〜70を介し
て制御装置61からモータ24゜35.46に回転制御
信号を出力すると、該各モータ24.35.46は前述
の混合比率に従って回転し、ポンプ21〜23,34.
45を回転駆動せしめる。この結果、主剤源15内のA
色の主剤は主剤配管12、ポンプ21、主剤弁5、マニ
ホールド2、主剤配管47、逆止弁51を介してライン
ミキサ50に供給され、硬化剤源32内の硬化剤は硬化
剤配管31、ポンプ34、硬化剤弁28、硬化剤配管4
8、逆止弁52を介してラインミキサ50に供給され、
さらに添加剤源43内の添加剤も添加剤配管42、ポン
プ45、添加剤弁39、添加剤配管49、逆止弁53を
介してラインミキサ50に供給される。そして、該ライ
ンミキサ50によって主剤、硬化剤、添加剤を混合する
ことによって得られた混合体は塗料パイプ54を介して
塗装枦55に供給され、該塗装機55から被塗物に向は
噴霧される。なお、この間ポンプ22.23も回転駆動
せしめられるが、主剤弁6,7は弁切換されていないか
ら、B色、0色の主剤は該各ポン7’22,23、主剤
配管13゜14、主剤弁6,7、戻シ配管12 ’、 
13の間を循環するのみである。
Next, control air is supplied to the main agent valve 5, curing agent valve 28, and additive valve 39 to switch the valves, and a rotation control signal is sent from the control device 61 to the motor 24° 35.46 via signal lines 68 to 70. , the motors 24, 35, 46 rotate according to the aforementioned mixing ratio, and the pumps 21-23, 34.
45 is rotated. As a result, A in the main agent source 15
The color main agent is supplied to the line mixer 50 via the main agent piping 12, pump 21, main agent valve 5, manifold 2, main agent piping 47, and check valve 51, and the hardening agent in the hardening agent source 32 is supplied to the hardening agent piping 31, Pump 34, curing agent valve 28, curing agent piping 4
8. Supplied to the line mixer 50 via the check valve 52,
Furthermore, the additive in the additive source 43 is also supplied to the line mixer 50 via the additive pipe 42 , the pump 45 , the additive valve 39 , the additive pipe 49 , and the check valve 53 . The mixture obtained by mixing the base agent, curing agent, and additives by the line mixer 50 is supplied to the coating tank 55 via the coating pipe 54, and is sprayed from the coating machine 55 onto the object to be coated. be done. During this time, the pumps 22 and 23 are also rotated, but since the main agent valves 6 and 7 are not switched, the main agents for colors B and 0 are pumped through the respective pumps 7' 22, 23, the main agent pipes 13, 14, Main agent valves 6, 7, return piping 12',
It only cycles between 13.

一方、ポンプ21.34.45の回転数は回転検出器5
6159160によってそれぞれ検出され、これらから
の供給量信号は信号線63 、66 。
On the other hand, the rotation speed of the pump 21.34.45 is detected by the rotation detector 5.
6159160, respectively, and supply amount signals from these are signal lines 63 and 66.

67を介して制御装置61に入力刻々入力される。Inputs are inputted to the control device 61 via 67 every moment.

この結果、該制御装置61は予め設定され記憶されてい
る所定の混合比率と、各回転検1」3器56゜59.6
0から入力される供給分イハ号とを常時比較し、この比
較結果にノルづいて信号線68 、69 。
As a result, the control device 61 adjusts the predetermined mixing ratio that has been set and stored in advance, and the
The signal lines 68 and 69 are constantly compared with the supply number Iha inputted from 0 and based on the comparison result.

70を介してモータ24. 、35 、46に所定の混
合比率を維持するための回転制御信号を出力し、回転数
を制御する。これにより、7j?ンプ21.34゜45
を所定の混合比率となるように回転駆動する。
Motor 24 . , 35, and 46 to control the rotation speed by outputting a rotation control signal for maintaining a predetermined mixing ratio. With this, 7j? 21.34°45
is rotated to achieve a predetermined mixing ratio.

なお、ポンプ22.23の回転検出器57.58からも
伊、給発信号が出力されているが、混合比率設定器62
からはA色の主剤についての混合比率のみが設定されて
いるから、これらの供給量信号についての比較は行なわ
れないり さらに、被塗物に対するA色の塗装作業が終了したら、
主剤弁5、硬化剤弁28、添加剤弁39への制御エアの
供給を停止して、これらを原切換位置に復帰さぜ、かつ
混合比集設定器62からのA色の主剤についての設定値
の入力をリセットする。
Incidentally, the feed signal is also output from the rotation detector 57.58 of the pump 22.23, but the mixing ratio setting device 62
Since only the mixing ratio for the base material of color A is set from , there is no comparison of these supply amount signals.
Stop the supply of control air to the main agent valve 5, curing agent valve 28, and additive valve 39, return these to their original switching positions, and set the A color main agent from the mixing ratio setting device 62. Reset value input.

然るに、反応硬化型塗料は月?ットライフを経過すると
硬化してし丑うから、早急に洗浄する必要がある。この
ため、塗装作業の終了後自動的にエア弁3に制御エアを
供給してこれを開弁じ、エア源9からのエアをエア配管
8を介してマニホールド2に供給し、主剤通路2A、主
剤配管47内のノ七−ジする。これが終了したら、シン
ナ弁4゜27.38にそれぞれ制御エアを供給してこれ
らを開弁し、ザーキュレーション・ぐイブ10.304
1からのシンナをシンナ配管g、29.40を介シてマ
ニホールド2,26.37にそれぞれ供給する。この結
果、該各マニホールド2.26゜37からのシンナは主
剤配管47.硬化剤配管48、添加剤49、逆止弁51
〜53、ラインミキサ50、塗料/4’イブ54をそれ
ぞれ介して塗装機55に供給され、これら内部を洗浄す
る。特に、逆止弁51〜53よシも下流側の各配管47
〜48、ラインミキサ50.塗料ノ(イブ54、塗装機
55には主剤と硬化剤との混合体が充満しているから、
これら内部を十分に洗浄する。さらに、主剤用のマニホ
ールド2、主剤配管47内にA色の主剤がわずかでも残
留すると、次回の塗装作業に際して色混り現象の虞れが
あるから、シンナによる洗浄終了後エア弁3に再び制御
エアを供給してこれを開弁し、エア源9からの洗浄用エ
アをエア配管8を介してマニホールド2に供給し、該マ
ニホールド2内と主剤配管47内に残留するA色の主剤
やシンナをパージすると共に乾燥し、さらに逆止弁51
、ラインミキサ50、塗料7′Pイブ54、塗装機55
内に残留する混合体やシンナをパージすると共に乾燥す
る。このようにして洗浄作業が終了するが必要に応じて
前述の工程を数回繰シ返すこと罠よって洗浄作業を行な
ってもよい。
However, is reaction curing paint the moon? It hardens after its dry life, so it needs to be cleaned as soon as possible. For this reason, after the completion of the painting work, control air is automatically supplied to the air valve 3 to open it, and air from the air source 9 is supplied to the manifold 2 via the air piping 8, and the main agent passage 2A, the main agent The inside of the pipe 47 is discharged. Once this is completed, supply control air to each of the thinner valves 4°27.38 to open them, and open the thinner valves 10.304.
Thinner from 1 is supplied to manifolds 2 and 26.37 via thinner pipes g and 29.40, respectively. As a result, the thinner from each manifold 2.26°37 is transferred to the main agent pipe 47. Hardening agent piping 48, additive 49, check valve 51
53, a line mixer 50, and a paint/4' tube 54, the paint is supplied to a coating machine 55, and the interior thereof is cleaned. In particular, each pipe 47 on the downstream side of the check valves 51 to 53
~48, line mixer 50. Since the paint sprayer 54 and the paint sprayer 55 are filled with a mixture of the main agent and hardener,
Thoroughly clean these insides. Furthermore, if even a small amount of the main agent of color A remains in the manifold 2 for the main agent and the main agent piping 47, there is a risk of color mixing during the next painting operation, so after cleaning with thinner is completed, the air valve 3 is again controlled. Air is supplied and the valve is opened, and cleaning air from the air source 9 is supplied to the manifold 2 through the air piping 8 to remove the A color base material and thinner remaining in the manifold 2 and the base material pipe 47. is purged and dried, and then the check valve 51 is
, line mixer 50, paint 7'P Eve 54, paint machine 55
Purge the mixture and thinner remaining inside and dry. The cleaning operation is completed in this way, but the cleaning operation may be carried out by repeating the above-mentioned steps several times as necessary.

以上によph色の主剤を用いた塗装作業と洗浄作業が終
了したことになるが、B色の主剤、6色の主剤を用いて
塗装作業を行なう場合にも、前述と同様に行なえばよい
ものである。
The painting work and cleaning work using the PH color main material have been completed above, but if you want to perform the painting work using the B color main material or the 6 color main materials, you can do the same as above. It is something.

次に、第2図は本発明の第2の実施例を示し、前述した
第1の実施例と同一構成要素には同一符号を付し、その
説明を省略する。
Next, FIG. 2 shows a second embodiment of the present invention, in which the same components as in the above-described first embodiment are designated by the same reference numerals, and their explanation will be omitted.

然るに、71.72.73,74.75は配管12.1
3,14,31.42の途中であってボンダ21.22
.23.′34.45の流出側にそれぞれ設けられた流
量計を示し、該各流量計71〜75には被測流量に比例
した流量信号を発信する流量発信器76.77.78,
79.80が装着され、該各流量発信器76〜80は信
号線81゜82.83,84.85を介して制御装置6
1と接続され、刻々の被測流量を入力しうるように構成
されている。
However, 71.72.73, 74.75 are piping 12.1
Bonda 21.22 in the middle of 3, 14, 31.42
.. 23. '34.45, each of which is equipped with a flow rate transmitter 76,77,78, which transmits a flow rate signal proportional to the measured flow rate.
79.80 is installed, and each flow rate transmitter 76-80 is connected to the control device 6 via signal lines 81, 82.83, 84.85.
1, and is configured so that the measured flow rate can be inputted every moment.

本実施例に用いる塗装装置は以上のよりに構成されるが
、第1の実施例における回転検出器56〜60からの供
給量信号に代えて流量発信器76〜80からの流量信号
に基づいて混合比率の制御を行なうものである点を除き
、その塗装方法については291の実施例と実質的に変
るところがない。
The coating apparatus used in this embodiment is constructed as described above, but is based on the flow rate signals from the flow rate transmitters 76 to 80 instead of the supply amount signals from the rotation detectors 56 to 60 in the first embodiment. The coating method is substantially the same as that of Example 291, except that the mixing ratio is controlled.

しかし、本実施例においてはポン7”21〜23゜34
.45の吐出側に流量n171〜75を挿入し、これら
によって直接流刀゛測定して混合比率の制御を行なうも
のであるから、より高精度な管理を行なうことができる
However, in this embodiment, the pon 7" is 21 to 23 degrees 34
.. Since the flow rates n171 to 75 are inserted into the discharge side of the pump 45 and the mixing ratio is controlled by directly measuring them, more accurate management can be achieved.

第3図は本発明の第3の実施例を示し、前述した第1の
実施例と同−構成要素には同一符号を伺してその説明を
省略する。
FIG. 3 shows a third embodiment of the present invention, in which the same components as those of the first embodiment described above are denoted by the same reference numerals, and their explanations will be omitted.

然るに、91は色替弁装置を示し、該色替弁装置91は
内部に通路92Aを41するマニホールド92と、流出
側が該通路92Aに接続されるエア弁3、シンツー弁4
、複数の主剤弁5 + 6 p 7 、硬化剤弁28お
よび添加剤弁39とカ・ら大略n・¥成さし、シカモ前
記マニボールド92の通l11592人の派出側は流出
用配管93を介してラインミキサ50の流入側と接総し
たことにおる。
However, 91 indicates a color change valve device, and the color change valve device 91 includes a manifold 92 having a passage 92A inside, an air valve 3 and a thin valve 4 whose outflow side is connected to the passage 92A.
, a plurality of main agent valves 5 + 6 p 7 , a hardening agent valve 28 and an additive valve 39 , and a plurality of main agent valves 5 + 6 p 7 , a curing agent valve 28 and an additive valve 39 , and the outflow side of the manibold 92 is The line mixer 50 is in contact with the inflow side of the line mixer 50.

本実施例に用いる塗装装置は以上のように構成サレるが
、第1の実施例における各マニホールド2,26.37
を1本のマニホールド92とすることKよシ、主剤供給
系統、硬化剤供給系統、添加剤供給系統を該マニホール
ド92に直接接続することができると共に、シンナ弁2
7.38を不要とすることができる。また、本実施例で
は流出用配管93内を主剤、硬化剤および添加剤が混合
しつつ流ハるから、ラインミキサ5oでの混合効果を高
めることができる。さらに、第1の実施例における逆止
弁51〜53を不要とすることができる。以上の各点を
除き混合比率制御を行ないつつ塗装を行なうものである
点について第1の実施例と変るところがない。
The coating device used in this embodiment has the configuration as described above, and each manifold 2, 26, 37 in the first embodiment
By using one manifold 92, the main agent supply system, hardening agent supply system, and additive supply system can be directly connected to the manifold 92, and the thinner valve 2 can be connected directly to the manifold 92.
7.38 can be made unnecessary. Further, in this embodiment, since the main agent, curing agent, and additive are mixed and flowed through the outflow pipe 93, the mixing effect in the line mixer 5o can be enhanced. Furthermore, the check valves 51 to 53 in the first embodiment can be made unnecessary. Except for the above points, this embodiment is the same as the first embodiment in that painting is performed while controlling the mixing ratio.

なお、前述の各実施例においては、主剤、硬化剤および
添加剤からなる3液性反応硬化型塗料を用いる場合につ
いて述べたが、この3液性塗料の場合には添加剤として
溶剤を用いる比較的低粘度のポリウレタン樹脂塗料や不
飽和ポリエステル樹脂塗料等の場合や、表面張力低下剤
、硬化遅延剤を混合する場合等に好適である。一方、厚
塗シ用の高粘度ハイソリッド形塗料や無溶剤形のポリウ
レタン樹脂塗料、エポキシ樹脂塗料等を用いてなる2液
性反応硬化型塗料の場合には、添加剤を不要とじつるも
のである。また、モータ24 、35゜46としては電
動モータに限ることなくエアモータを用いてもよく、こ
の場合には電空変換器を介在させればよい。まだ、硬化
剤切換弁装置25、添加剤切換弁装置36にエア弁を設
りる構成としてもよい。さらに、混合手段としてライン
ミキサ50を用いるものとして述べたが、ポットライフ
が短かい塗料ではミキシング機構を塗装機55の内部に
備えてなる内部混合式の塗装機としてもよいものである
。さらに、主剤源15〜17内にはA色、B色、C色の
主剤を貯えておくものとして述べたが、例えばポリウレ
タン樹脂塗料、エポキシ樹脂塗料、不飽和ポリエステル
樹脂塗料等、異種の主剤を貯えておくものであってもよ
い。さらにまた、第3の実施例において回転検出器56
〜60に代えて、第2の実施例の如く流量計71〜75
を用いてもよいことは勿論である。。
In addition, in each of the above-mentioned examples, a case was described in which a three-component reaction-curing paint consisting of a base agent, a curing agent, and an additive was used. It is suitable for use with low-viscosity polyurethane resin paints, unsaturated polyester resin paints, etc., and when mixing surface tension lowering agents and curing retarders. On the other hand, in the case of two-component reaction-curing paints that use high-viscosity, high-solid paints for thick coatings, solvent-free polyurethane resin paints, epoxy resin paints, etc., additives are not required. be. Further, the motors 24 and 35.degree. 46 are not limited to electric motors, but air motors may be used, and in this case, an electro-pneumatic converter may be used. Alternatively, the curing agent switching valve device 25 and the additive switching valve device 36 may be provided with air valves. Furthermore, although the line mixer 50 is used as the mixing means, for paints with a short pot life, an internal mixing type atomizer in which the mixing mechanism is provided inside the atomizer 55 may be used. Furthermore, although it has been described that the base agents of colors A, B, and C are stored in the base agent sources 15 to 17, different types of base agents such as polyurethane resin paint, epoxy resin paint, unsaturated polyester resin paint, etc. It may be something to store. Furthermore, in the third embodiment, the rotation detector 56
~60, flowmeters 71~75 as in the second embodiment
Of course, it is also possible to use .

本発明に係る反応硬化型塗料の塗装方法は以上詳細に述
べた如くであって、各供給系統から供給されている供給
量を検出しつつ混合比率を制御するようにしだから、供
給量の変動、外囲条件の変化等があっても、常時高精度
な混合比率を確保することができ、また自動色替えない
しは自動主剤替えを簡単に行なうことができる等の効果
を奏する。
The method for applying a reaction-curing paint according to the present invention is as described above in detail, and since the mixing ratio is controlled while detecting the amount of supply supplied from each supply system, fluctuations in the amount of supply, Even if there are changes in the surrounding conditions, a highly accurate mixing ratio can be maintained at all times, and automatic color changes or automatic base agent changes can be easily performed.

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

第1図は本発明に用いる第1の実施例を示す系統図、第
2図は同じく第2の実施例に用いる系統図、第3図は同
じく第3の実施例に用いる系統図である。 1.91・・・色替弁装置、11,30,41・・・シ
ンナ源、12,13,14,47・・・主剤配管、15
.16,17・・・主剤源、21,22,23゜34.
45・・・ポンプ、24,35.46・・・モータ、2
5・・・硬化剤切換弁装置、31.48・・・硬化剤配
管、32・・・硬化剤源、36・・・添加剤切換弁装置
、42 、49・・・添加剤配管、43・・・添加剤源
、50・・・ラインミキサ、54・・・塗料パイプ、5
5・・・塗装機、56,57,58,59.60・・・
回転検出器、61・・・制御装置、62・・・混合比率
設定器、71゜72.73,74,75・・・流量計、
76.77゜78.79.80・・・流量発信器。
FIG. 1 is a system diagram showing a first embodiment used in the present invention, FIG. 2 is a system diagram similarly used in the second embodiment, and FIG. 3 is a system diagram similarly used in the third embodiment. 1.91...Color change valve device, 11,30,41...Thinner source, 12,13,14,47...Main agent piping, 15
.. 16,17...Main agent source, 21,22,23°34.
45...Pump, 24,35.46...Motor, 2
5... Curing agent switching valve device, 31.48... Curing agent piping, 32... Curing agent source, 36... Additive switching valve device, 42, 49... Additive piping, 43. ...Additive source, 50...Line mixer, 54...Paint pipe, 5
5... Painting machine, 56, 57, 58, 59.60...
Rotation detector, 61... Control device, 62... Mixing ratio setting device, 71° 72.73, 74, 75... Flow meter,
76.77°78.79.80...Flow rate transmitter.

Claims (2)

【特許請求の範囲】[Claims] (1)主剤供給系統と硬化剤供給系統からそれぞれ供給
される主剤と硬化剤とを混合することによって混合体と
なし、この混合体を検装機から被塗物に向けて噴霧する
ようにしてなる反応硬化型塗料の塗装方法において、前
記主剤供給系統と硬化剤供給系統からそれぞれ供給され
ている供給量を検出し、当該主剤と硬化剤の供給圧出と
予め設定された混合圧出とを比較し、前記主剤と硬化剤
の供給量を予め設定された混合圧出となるように制御す
るように構成したことを特徴とする反応硬化型塗料の塗
装方法。
(1) A mixture is made by mixing the base agent and hardener supplied from the base agent supply system and the hardener supply system, respectively, and this mixture is sprayed from the inspection machine toward the object to be coated. In this reaction-curing paint coating method, the supply amounts supplied from the base agent supply system and the curing agent supply system are detected, and the supply pressure and the preset mixing pressure of the base resin and curing agent are controlled. In comparison, a method for applying a reaction-curing paint is characterized in that the supply amount of the base agent and curing agent is controlled so as to achieve a preset mixed pressure.
(2)主剤供給系統、硬化剤供給系統および添加剤供給
系統からそれぞれ供給される主剤、硬化剤および添加剤
を混合することによってこれらの混合体となし、この混
合体を塗装機から被塗物に向けて噴霧するようにしてな
る反応硬化型塗料の塗装方法において、前記主剤供給系
統、硬化剤供給系統および添加剤供給系統からそれぞれ
供給されている供給」°を検出し、当該検出量と予め設
定された混合圧出とを比較し、前記主剤、硬化剤および
添加剤の供給量を予め設定された混合圧出となるように
制御するように構成したことを特徴とする反応硬化型塗
料の塗装方法。
(2) A mixture of the base agent, hardener, and additives supplied from the base agent supply system, curing agent supply system, and additive supply system is made by mixing them, and this mixture is transferred from the coating machine to the object to be coated. In a method for applying a reaction-curing paint in which the paint is sprayed toward A reaction-curing paint characterized in that the supply amount of the base agent, curing agent, and additive is controlled so as to achieve a preset mixture extrusion by comparing the extrusion mixture with a preset extrusion mixture. Painting method.
JP8539883A 1983-05-16 1983-05-16 Painting method of reaction curing type Granted JPS59213468A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8539883A JPS59213468A (en) 1983-05-16 1983-05-16 Painting method of reaction curing type

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8539883A JPS59213468A (en) 1983-05-16 1983-05-16 Painting method of reaction curing type

Publications (2)

Publication Number Publication Date
JPS59213468A true JPS59213468A (en) 1984-12-03
JPH0318502B2 JPH0318502B2 (en) 1991-03-12

Family

ID=13857665

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8539883A Granted JPS59213468A (en) 1983-05-16 1983-05-16 Painting method of reaction curing type

Country Status (1)

Country Link
JP (1) JPS59213468A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62294458A (en) * 1986-06-12 1987-12-21 Toyota Motor Corp Method for controlling emitting quantity of much-liquid coater
JPH03196861A (en) * 1989-03-13 1991-08-28 Behr Ind Equip Inc Electrostatic spray coating device and method for coating mixture of two components
JPH0474553A (en) * 1990-07-16 1992-03-09 Aica Kogyo Co Ltd Cleaning device for two liquid mixing and discharging machine
JPH07185409A (en) * 1993-12-27 1995-07-25 Tokioka Techno Service:Kk Two-part liquid mixing type spray device
JP2008049294A (en) * 2006-08-25 2008-03-06 Asahi Sunac Corp Two-pack coating apparatus
WO2008081634A1 (en) 2006-12-27 2008-07-10 Abb K.K. Painting apparatus

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57165068A (en) * 1981-04-03 1982-10-09 Dainippon Toryo Co Ltd Coating method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57165068A (en) * 1981-04-03 1982-10-09 Dainippon Toryo Co Ltd Coating method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62294458A (en) * 1986-06-12 1987-12-21 Toyota Motor Corp Method for controlling emitting quantity of much-liquid coater
JPH03196861A (en) * 1989-03-13 1991-08-28 Behr Ind Equip Inc Electrostatic spray coating device and method for coating mixture of two components
JPH0474553A (en) * 1990-07-16 1992-03-09 Aica Kogyo Co Ltd Cleaning device for two liquid mixing and discharging machine
JPH07185409A (en) * 1993-12-27 1995-07-25 Tokioka Techno Service:Kk Two-part liquid mixing type spray device
JP2008049294A (en) * 2006-08-25 2008-03-06 Asahi Sunac Corp Two-pack coating apparatus
WO2008081634A1 (en) 2006-12-27 2008-07-10 Abb K.K. Painting apparatus

Also Published As

Publication number Publication date
JPH0318502B2 (en) 1991-03-12

Similar Documents

Publication Publication Date Title
US6896152B2 (en) Electronic plural component proportioner
US4915599A (en) Coating material supply device
EP0662015B1 (en) Method and apparatus for preparing mixtures with compressed fluids
JPS63305955A (en) Pump operation type paint spray apparatus
US3216622A (en) Method of controlling the quantities discharged during predetermined periods of one or more viscous liquids and apparatus for performing the method
US4714179A (en) Positive displacement paint pushout apparatus
JPS59213468A (en) Painting method of reaction curing type
KR101214721B1 (en) Proportional apparatus for plural component coating pump
US5961300A (en) Diaphragm pump plural component dispensing system with integrator
JP4375858B2 (en) Multi-liquid mixing control method
JP2008302315A (en) Apparatus for supplying coating material, and method of coating
MXPA00007059A (en) Mixing block for mixing multi-component reactive material coating systems and an apparatus using same.
JPH0316186B2 (en)
US20040165476A1 (en) Two component coating mixing system
US6601733B1 (en) Multi-component proportioning system and delivery system utilizing same
KR20030024687A (en) Method for production and spray-application of a multicomponent paint
JPS6343147B2 (en)
JP2004154643A (en) Multi-liquid mixing apparatus, and multi-liquid mixing method
JPH0626710B2 (en) Discharge rate control method for multi-liquid coating equipment
JP3117688U (en) Two-component paint coating equipment
CN217594525U (en) Two ingredient coating ratio metering device
JPH03127657A (en) Mixer in two-pack pressure mixing sprayer for adhesive or the like
JPH054147B2 (en)
JPH0290963A (en) Device for changing color in coating
Muir Plural-Component proportioners