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JPH074569B2 - Drying method for alkyd resin paint - Google Patents
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JPH074569B2 - Drying method for alkyd resin paint - Google Patents

Drying method for alkyd resin paint

Info

Publication number
JPH074569B2
JPH074569B2 JP61049151A JP4915186A JPH074569B2 JP H074569 B2 JPH074569 B2 JP H074569B2 JP 61049151 A JP61049151 A JP 61049151A JP 4915186 A JP4915186 A JP 4915186A JP H074569 B2 JPH074569 B2 JP H074569B2
Authority
JP
Japan
Prior art keywords
drying
air
resin paint
furnace
drying chamber
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 - Fee Related
Application number
JP61049151A
Other languages
Japanese (ja)
Other versions
JPS62204882A (en
Inventor
芳夫 荻野
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP61049151A priority Critical patent/JPH074569B2/en
Publication of JPS62204882A publication Critical patent/JPS62204882A/en
Publication of JPH074569B2 publication Critical patent/JPH074569B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、アルキッド樹脂塗料などのような常温または
強制乾燥で乾燥硬化する常温乾燥型または強制乾燥型塗
料の乾燥方法にに関するものである。
TECHNICAL FIELD The present invention relates to a method for drying an ordinary temperature drying type or forced drying type coating which is dried and cured at ordinary temperature or forced drying such as an alkyd resin coating.

〔従来の技術〕[Conventional technology]

通常、塗装物品の乾燥には多くは連続式の乾燥炉が使用
され、炉の一方の口(入口)より塗装物品を送入し、炉
内で加熱乾燥または硬化したのち、炉の他方の口(出
口)から外部へ出てくるようになっている。
Usually, a continuous drying oven is often used to dry the coated article. The coated article is fed from one port (inlet) of the oven, and is heated and dried or cured in the oven, and then the other port of the oven is dried. It comes out from the (exit).

しかしながら、建設機械,重車輌,大型車輌,重電機製
品などの大型塗装物の乾燥には、上記連続式の乾燥炉で
は、大きな乾燥炉が必要となり、また製品の部分に比較
的高温に耐えない箇所がある場合があり、さらに熱容量
の大き部分があって加熱乾燥に長時間を要するので、ア
ルキッド樹脂塗料およびウレタン系樹脂塗料などのよう
な空気中で乾燥硬化(酸化重合または酸化硬化)する常
温乾燥型または強制乾燥型塗料が用いられている。
However, in order to dry large paints such as construction machinery, heavy vehicles, large vehicles, and heavy electrical equipment products, a large drying oven is required in the above continuous drying oven, and the product portion cannot withstand relatively high temperatures. Since there are some places and there is a large part of the heat capacity and it takes a long time to heat and dry, it is dry and hardened (oxidative polymerization or oxidative hardening) in air like alkyd resin paints and urethane resin paints at room temperature. Dry or forced drying paints are used.

このアルキッド樹脂塗料(その変性樹脂塗料を含む)
は、酸化重合型塗料であるため、常温放置の場合乾燥に
は時間がかかり、完全硬化には数日間を必要とする場合
もある。そのため、塗装物を次工程に移すに最低必要と
される塗膜の指触乾燥までにも或る程度の時間を必要と
する。
This alkyd resin paint (including its modified resin paint)
Since it is an oxidative polymerization type coating, it takes a long time to dry when left at room temperature, and it may take several days for complete curing. Therefore, a certain amount of time is required until the coating film is touch-dried, which is the minimum required to transfer the coated product to the next step.

実際問題として生産ラインにおける塗装では、上塗塗装
の場合にはマスキングなどのためのテーピングが必要の
場合もある。また乾燥時間が長いとゴミの付着、装置の
占有時間が長い。よって、生産ラインのタクトの向上、
テーピングまでの時間の短縮、乾燥までのゴミ付着の防
止などのため強制乾燥を必要としていた。
As a practical matter, taping for masking or the like may be necessary in the case of top-coating in the case of painting in a production line. Further, if the drying time is long, dust adheres and the device occupies long time. Therefore, the tact of the production line is improved,
Forced drying was required to reduce the time required for taping and to prevent dust from adhering until drying.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

この大型製品の強制乾燥については、従来の生産ライン
では電気赤外線炉または電気遠赤外線炉による加熱が広
く採用されていた。しかしながら、この電気赤外線方式
または電気遠赤外線方式によるときは、電力消費量が膨
大で省エネルギーに反すること、また赤外線は直進形な
ので影となる部分が加熱できず全面的に加熱乾燥しなけ
ればならないこと、更にアルキッド樹脂塗料などは酸化
重合型であるため塗膜面への酸素の接触が必要であるこ
となどから、乾燥には長時間を必要とした。
Regarding the forced drying of this large product, heating by an electric infrared furnace or an electric far infrared furnace has been widely adopted in the conventional production line. However, when this electric infrared method or electric far infrared method is used, the power consumption is enormous and it is against energy saving. Also, since the infrared ray is a straight type, the shadowed part cannot be heated and must be completely dried by heating. Further, since the alkyd resin paint and the like are of an oxidative polymerization type, it is necessary to bring oxygen into contact with the surface of the coating film, so that it took a long time to dry.

上記の理由から、簡単な乾燥炉でしかも短時間で仕上り
性よく酸化重合型塗料を乾燥させる方法が望まれてい
た。
For the above reasons, there has been a demand for a method of drying an oxidation-polymerization type coating material in a simple drying furnace in a short time with good finish.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者は、酸化重合型塗料の乾燥には、加熱のみでは
不十分で、十分量の酸素との接触、特に加熱後の冷空気
との接触が重要である点に着目して本発明を完成した。
The present inventors have focused on the present invention by focusing on the point that contacting with a sufficient amount of oxygen, particularly contact with cold air after heating is important for drying the oxidative polymerization type paint, only by heating. completed.

本発明の常温乾燥型または強制乾燥型塗料の乾燥方法
は、アルキッド樹脂塗料(またはその変性樹脂)塗料お
よびウレタン系樹脂塗料などの常温乾燥型または強制乾
燥型塗料を塗布した塗装物を乾燥室に入れ、該乾燥室内
に燃焼加熱空気を送入して塗装物を所定の温度に加熱し
たのち、該乾燥室内に空気を送入して塗装物を冷却する
ことからなることを特徴とする。
The method for drying a room-temperature-drying type or forced-drying-type coating material according to the present invention is a method of drying a coated article to which a room-temperature-drying type or forced-drying type coating material such as an alkyd resin coating material (or its modified resin) coating material and a urethane resin coating material is applied. It is characterized in that it is configured such that combustion heating air is fed into the drying chamber to heat the coated article to a predetermined temperature, and then air is fed into the drying chamber to cool the coated article.

本発明は、酸化重合型または加熱して冷却すると塗膜が
「しまる(締る)」型の常温乾燥型または強制乾燥型塗
料であればいずれのものも適用できるが、特にフタール
酸樹脂塗料のようなアルキッド樹脂およびウレタン系樹
脂塗料が好ましい。
In the present invention, any coating can be applied as long as it is an oxidative polymerization type or a room temperature drying type or a forced drying type coating in which the coating film "clamps" when heated and cooled. Alkyd resin and urethane resin coatings such as

本発明は、乾燥室として1室(1ルーム)型のもの、例
えばガス燃焼熱風循環式バッチ炉を用い、この1基の炉
内に塗装物を入れ、ガスバーナーによる燃焼加熱空気
(熱風)を炉内に送入循環させて短時間で塗装物を均熱
加熱し、一定時間経過後に熱風循環経路を「閉」にし、
外気導入ダンパを「開」、大量排気ダクトを「開」と
し、外気の冷風を大量に塗装物(製品)に当てて冷却
し、炉内の加熱空気は大量排気ダクトによって炉外に排
気することによって行う。
The present invention uses a one-room type drying chamber, for example, a gas combustion hot air circulation type batch furnace, in which the coating material is put in one furnace and combustion heating air (hot air) by a gas burner is supplied. Introduces and circulates in the furnace to uniformly heat the coated object in a short time, and after a certain period of time, closes the hot air circulation path,
Open the outside air introduction damper and open the large-volume exhaust duct, cool a large amount of cold air of the outside air to the coating object (product) to cool, and exhaust the heated air in the furnace to the outside of the furnace by the large-volume exhaust duct. Done by.

本発明で使用する乾燥炉において、送風機は加熱のとき
と空冷のときのいづれにも同一のものを用いることがで
き、大容量の循環ファン(送風機)を使用することによ
って1基のファンとすることができる。
In the drying furnace used in the present invention, the same blower can be used both for heating and for air cooling, and a large-capacity circulation fan (blower) is used to form one fan. be able to.

大型重車輌,大型重電機器などの塗装物の加熱は、アル
キッド樹脂塗料の場合は、90℃位にて短時間焼付型熱風
炉で20〜30分間位で塗装物全体を加熱することができ
る。
For the heating of coated objects such as large heavy vehicles and large heavy electrical equipment, in the case of alkyd resin paint, the entire coated object can be heated in about 20 to 30 minutes in a short-time baking hot air oven at about 90 ° C. .

本発明の塗料の乾燥方法によれば、乾燥炉内の塗装物の
加熱−冷却のほかに、乾燥炉自体の乾燥室内の温度を急
速に所定の温度に加熱し冷却することができる。
According to the coating material drying method of the present invention, in addition to heating and cooling the coating material in the drying furnace, the temperature in the drying chamber of the drying furnace itself can be rapidly heated to a predetermined temperature and cooled.

したがって本発明は、更に、塗装物乾燥時などの所要時
に乾燥室内に燃焼加熱空気を送入して該室内を所定温度
に加熱し、乾燥室内冷却時には該室内に乾燥室外の空気
を送入することからなる乾燥室内の急速加熱−冷却方法
に関するものである。
Therefore, according to the present invention, combustion heating air is further fed into the drying chamber to heat the chamber to a predetermined temperature when required such as when drying a coated object, and when the drying chamber is cooled, air outside the drying chamber is fed into the chamber. The present invention relates to a rapid heating-cooling method in a drying chamber.

〔実施例〕〔Example〕

以下、本発明を実施例により説明するが、本発明はこれ
に限定されるものではない。
Hereinafter, the present invention will be described by way of examples, but the present invention is not limited thereto.

第1図は乾燥炉の正面断面図、第2図は平面図で、1は
乾燥炉本体、2は熱風送入ダクト、3は熱風等循環用ダ
クト、4は外気取入用ダクト、5a,5bはダンパー、6は
排気ダクト、7はバーナー燃焼装置、8は塗装物、9は
送風機、10はモーター、21は熱風吹出口を示す。
FIG. 1 is a front sectional view of the drying furnace, FIG. 2 is a plan view, 1 is a drying furnace main body, 2 is a hot air inlet duct, 3 is a hot air circulation duct, 4 is an outside air intake duct, 5a, 5b is a damper, 6 is an exhaust duct, 7 is a burner combustion device, 8 is a painted object, 9 is a blower, 10 is a motor, and 21 is a hot air outlet.

乾燥は次のようにして行った。Drying was performed as follows.

アルキッド樹脂塗料など例えばフタール酸樹脂塗料にて
塗装後の塗装物(製品)8を、入口扉を開けて炉本体1
内に搬入し、扉を閉じたのち操作盤の押ボタン操作にて
バーナー燃焼装置7のパイロットバーナー、メインバー
ナーを着火させて熱風を生じさせ、生じた熱風を熱風送
入用ダクト2で炉本体1内に送入する。ダクト2の熱風
吹出口21より炉内に吹出された熱風は、塗装物8に直接
または間接に熱を伝え熱風循環用ダクト3より吸込ま
れ、バーナー燃焼装置7を経て熱風送入用ダクト2によ
り再び炉本体1内に送入される。この間、外気取入用ダ
クト4のダンパー5aおよび排気ダクト6のダンパー(図
示せず)は「閉」としておく。
Open the entrance door and open the furnace door 1 of the product (product) 8 that has been painted with phthalic resin paint, such as alkyd resin paint.
After carrying in the inside and closing the door, the pilot burner and the main burner of the burner combustion device 7 are ignited by the push button operation of the operation panel to generate hot air, and the generated hot air is fed into the hot air feeding duct 2 in the furnace main body. Send within 1. The hot air blown into the furnace from the hot air outlet 21 of the duct 2 transfers heat directly or indirectly to the coating object 8 and is sucked from the hot air circulation duct 3 and passes through the burner combustor 7 and the hot air inlet duct 2 It is again fed into the furnace body 1. During this time, the damper 5a of the outside air intake duct 4 and the damper (not shown) of the exhaust duct 6 are kept "closed".

本例の場合、炉内温度調節器を90℃に設定し、90℃に昇
温後この温度で25分間保持したのち、メインバーナー、
パイロットバーナーが燃焼停止となり、次に循環回路の
ダンパー5bが「閉」、外気取入用ダクトおよび排気ダク
トの各ダンパーがそれぞれ「開」となるようにして塗装
物8を空冷した。本例の場合、空冷時間は20分間とし
た。
In the case of this example, the temperature controller in the furnace is set to 90 ° C., and after raising the temperature to 90 ° C. and holding at this temperature for 25 minutes, the main burner,
The pilot burner stopped burning, then the damper 5b of the circulation circuit was "closed" and the dampers of the outside air intake duct and the exhaust duct were each "open", and the coated object 8 was air-cooled. In this example, the air cooling time was 20 minutes.

炉本体1内に所定時間外気を送入して塗装物8を空冷し
たのちは、外気取入用ダクトおよび排気ダクトの各ダン
パーは「閉」、循環回路のダンパー5bは「開」となるよ
うにして全操作を終了する。なお、バーナー燃焼装置お
よび送風機の作動、各ダンパーの開・閉等は全て自動制
御とすると有利である。
After the outside air is sent into the furnace body 1 for a predetermined time to cool the coated object 8 by air, the dampers of the outside air intake duct and the exhaust duct are “closed”, and the damper 5b of the circulation circuit is “open”. And complete all operations. It should be noted that it is advantageous to automatically control the operation of the burner combustion device and the blower, and the opening / closing of each damper.

本例の場合、加熱から空冷操作の終了まで約40〜45分で
あり、従来の方法に比べるとはるかに短縮されており、
乾燥工程後の製品表面のアルキッド樹脂塗料は、加熱さ
れた酸素との接触とその後の冷却効果により非常によく
「しまり」、硬化が良好でその後のテーピング(マスキ
ング)は勿論のこと、生産性の向上、耐久性、耐候性に
優れた塗膜が得られた。
In the case of this example, it takes about 40 to 45 minutes from the heating to the end of the air cooling operation, which is much shorter than the conventional method,
The alkyd resin paint on the surface of the product after the drying process "tightens" very well due to the contact with heated oxygen and the cooling effect after that, and the curing is good, and not only the taping (masking) after that but also the productivity A coating film excellent in improvement, durability and weather resistance was obtained.

〔発明の効果〕〔The invention's effect〕

本発明の乾燥方法によれば、熱風を乾燥室内に送入して
塗装物を加熱するため、従来の赤外線方式の加熱のよう
に影になる部分がなく、塗装物全体を均一に加熱するこ
とができる。
According to the drying method of the present invention, since hot air is sent into the drying chamber to heat the coated article, there is no shadowed portion as in conventional infrared heating, and the entire coated article can be heated uniformly. You can

加熱源として、ガス燃焼空気を直接用いるため、エネル
ギー的にも損失が少く、また直接塗装面に熱風が当るよ
うにしているので、更に加熱時間を短縮することができ
ている。さらに大量の加熱、冷却空気を塗膜に当てるこ
とにより酸化重合もはやく進行することから、この点か
らも有利である。
Since the gas combustion air is directly used as the heating source, the energy loss is small, and the hot air is directly applied to the coated surface, so that the heating time can be further shortened. It is also advantageous from this point that the oxidative polymerization will proceed further by applying a large amount of heating and cooling air to the coating film.

酸化重合型塗料の場合、高温に加熱する必要もなく、ま
た加熱−冷却時間も送風量によって短かくできるため、
ワンルーム(1室)型の乾燥室で熱風と冷風を入れ換え
るだけでよい。このようにバッチ型乾燥室による短時間
の加熱−空冷であるため、ゴミの付着等が見られず、塗
膜の艶も失われず、鮮映性の良好な仕上り品が得られ
る。
In the case of oxidative polymerization type paint, it is not necessary to heat it to a high temperature, and the heating-cooling time can be shortened by the air flow rate,
It is sufficient to switch hot air and cold air in a one-room type drying room. As described above, since heating is performed in a batch type drying chamber for a short period of time and air cooling is performed, adhesion of dust and the like is not observed, gloss of the coating film is not lost, and a finished product having good sharpness can be obtained.

本発明の乾燥室の急速加熱−冷却方法によれば、乾燥室
内を急速に所定の温度に加熱できかつ所定の温度に冷却
できるので、バッチ方式またはトンネル方式の炉のい
づれを問わず、1基の乾燥炉で種々の焼付け温度の異な
る塗料の焼付・乾燥を行うことができ、また強制乾燥
型塗料や焼付乾燥型塗料など乾燥性質の異なる塗料の焼
付・乾燥を行うことができる。このほか、例えばトン
ネル炉でコンベアから塗装物(製品)などが落下したな
どで作業者が炉内に入る場合などに急速に炉内を冷却で
き、その後所定の温度に急速に戻すことができるなど、
多くの利点を有する。なお、本発明の性質上、トンネル
炉はエアカーテンなどの適当な手段で両端が外気と遮断
された形式の炉が用いられる。
According to the rapid heating-cooling method of the drying chamber of the present invention, since the drying chamber can be rapidly heated to a predetermined temperature and cooled to a predetermined temperature, one unit is used regardless of whether the furnace is a batch system or a tunnel system. In this drying furnace, it is possible to bake / dry various paints having different baking temperatures, and it is also possible to bake / dry paints having different drying properties such as forced-drying type paints and baking-drying type paints. In addition, the inside of the furnace can be rapidly cooled, for example, when a worker enters the furnace due to the fall of coated objects (products) in the tunnel furnace, and then the temperature can be quickly returned to a predetermined temperature. ,
It has many advantages. Due to the nature of the present invention, the tunnel furnace is a furnace of which both ends are shielded from the outside air by an appropriate means such as an air curtain.

装置的には1ルームの乾燥室なので、特別な空冷装置等
も不要で、従来の炉に自動ダンパーを3ケ所程度と、外
気取入用ダクト、大容量排気ダクトを設けるだけでよい
ため、設備費も安価であり、特別のスペースも必要ない
という利点を有する。
Since the equipment is a one-room drying room, no special air-cooling device is required, and only three automatic dampers, outside air intake ducts, and large-capacity exhaust ducts need to be installed in the conventional furnace. It has the advantages of low cost and no special space required.

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

第1図は乾燥炉の一例を示す正面断面図、 第2図は同乾燥炉の平面図である。 図中、 1…乾燥炉本体、2…熱風送入ダクト 3…循環用ダクト、4…外気取入用ダクト 5a,5b…ダンパー、6…排気ダクト 8…塗装物、 FIG. 1 is a front sectional view showing an example of a drying furnace, and FIG. 2 is a plan view of the drying furnace. In the figure, 1 ... Drying oven main body, 2 ... Hot air inlet duct 3, Circulation duct, 4 ... Outside air intake duct 5a, 5b ... Damper, 6 ... Exhaust duct 8 ... Painted object,

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】アルキッド樹脂塗料(その変性樹脂塗料を
含む)およびウレタン系樹脂塗料などの酸化重合型塗料
を塗布した塗装物を乾燥室に入れ、該乾燥室内に燃焼加
熱空気を送入して塗装物を所定の温度に加熱したのち、
該乾燥室内に乾燥室外の空気を送入して塗装物を冷却す
ると共に酸化硬化させることを特徴とする酸化重合型塗
料の乾燥方法。
1. An article coated with an oxidative polymerization type paint such as an alkyd resin paint (including its modified resin paint) and a urethane resin paint is placed in a drying chamber, and combustion heating air is fed into the drying chamber. After heating the coated object to the specified temperature,
A method for drying an oxidative polymerization type coating material, characterized in that air outside the drying room is sent into the drying room to cool the coated article and oxidatively cure it.
【請求項2】乾燥室が1室よりなることを特徴とする特
許請求の範囲第1項記載の乾燥方法。
2. The drying method according to claim 1, wherein the drying chamber comprises one chamber.
【請求項3】酸化重合型塗料がフタール酸樹脂塗料など
のアルキッド樹脂塗料であることを特徴とする特許請求
の範囲第1項記載の乾燥方法。
3. The drying method according to claim 1, wherein the oxidative polymerization type paint is an alkyd resin paint such as a phthalic acid resin paint.
【請求項4】乾燥室内への燃焼加熱空気の送入および乾
燥室外の空気の送入を1基の大容量循環ファンで行うこ
とを特徴とする特許請求の範囲第1項記載の乾燥方法。
4. The drying method according to claim 1, wherein the combustion heating air is fed into the drying chamber and the air outside the drying chamber is fed by one large capacity circulation fan.
【請求項5】燃焼加熱空気がバーナーによるガス燃焼加
熱空気であることを特徴とする特許請求の範囲第1項記
載の乾燥方法。
5. The drying method according to claim 1, wherein the combustion heating air is gas combustion heating air by a burner.
【請求項6】大容量循環ファンによる乾燥室外の空気の
送入によって乾燥室内を急速冷却することを特徴とする
特許請求の範囲第1項記載の乾燥方法。
6. The drying method according to claim 1, wherein the inside of the drying chamber is rapidly cooled by sending in air outside the drying chamber by a large capacity circulation fan.
JP61049151A 1986-03-06 1986-03-06 Drying method for alkyd resin paint Expired - Fee Related JPH074569B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61049151A JPH074569B2 (en) 1986-03-06 1986-03-06 Drying method for alkyd resin paint

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61049151A JPH074569B2 (en) 1986-03-06 1986-03-06 Drying method for alkyd resin paint

Publications (2)

Publication Number Publication Date
JPS62204882A JPS62204882A (en) 1987-09-09
JPH074569B2 true JPH074569B2 (en) 1995-01-25

Family

ID=12823096

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61049151A Expired - Fee Related JPH074569B2 (en) 1986-03-06 1986-03-06 Drying method for alkyd resin paint

Country Status (1)

Country Link
JP (1) JPH074569B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55132664A (en) * 1979-03-31 1980-10-15 Sumitomo Metal Ind Ltd Method and apparatus for baking of coated pipe
JPH0240389B2 (en) * 1982-10-08 1990-09-11 Daihatsu Motor Co Ltd JIDOSHABODEEYOSHIIRINGUZAINOKOKAHO

Also Published As

Publication number Publication date
JPS62204882A (en) 1987-09-09

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