JPH0333386B2 - - Google Patents
Info
- Publication number
- JPH0333386B2 JPH0333386B2 JP222585A JP222585A JPH0333386B2 JP H0333386 B2 JPH0333386 B2 JP H0333386B2 JP 222585 A JP222585 A JP 222585A JP 222585 A JP222585 A JP 222585A JP H0333386 B2 JPH0333386 B2 JP H0333386B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- combustion gas
- hot air
- circulation path
- duct
- 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
Links
- 238000010438 heat treatment Methods 0.000 claims description 38
- 239000000567 combustion gas Substances 0.000 claims description 34
- 238000001035 drying Methods 0.000 claims description 34
- 239000003973 paint Substances 0.000 claims description 12
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 238000010422 painting Methods 0.000 claims description 4
- 239000011248 coating agent Substances 0.000 description 12
- 238000000576 coating method Methods 0.000 description 12
- 239000000126 substance Substances 0.000 description 10
- 230000032798 delamination Effects 0.000 description 8
- 239000000446 fuel Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000003960 organic solvent Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000004383 yellowing Methods 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- -1 amine compounds Chemical class 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000004848 polyfunctional curative Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Coating Apparatus (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本願発明は、炉内に熱風を循環対流させて被塗
物を加熱乾燥させる熱風循環式の塗装用乾燥炉及
びその加熱方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a hot air circulation type coating drying furnace for heating and drying an object to be coated by circulating and convecting hot air in the furnace, and a heating method thereof.
この種の塗装用乾燥炉は、重油、灯油、都市ガ
スあるいはLPガス等の燃料をバーナで燃焼させ
て発生した燃焼ガスを直接炉内に循環対流させる
直接加熱式(直火式)の乾燥炉と、バーナの燃焼
ガスを燃焼ガス−空気熱交換器に送り込んで空気
を加熱し加熱された熱空気を炉内に循環対流させ
る間接加熱式(熱交換式)の乾燥炉とに大別する
ことができる。
This type of paint drying oven is a direct heating type (direct-fire type) drying oven that circulates and convects the combustion gas generated by burning fuel such as heavy oil, kerosene, city gas, or LP gas in a burner. and indirect heating type (heat exchange type) drying furnaces, in which the combustion gas from the burner is sent to a combustion gas-air heat exchanger to heat the air, and the heated hot air is circulated and convected within the furnace. Can be done.
ここで、直接加熱式の乾燥炉は、熱交換による
熱の損失がなく炉内に直接燃焼ガスが導入される
ために熱効率が非常に良く炉内温度を速やかに上
昇させることができるという長所がある反面、燃
焼ガスに含まれた塵埃、不純物等により被塗物の
製品品質に悪影響を与えるという欠点がある。特
に、石油系の燃料を使用する場合には硫黄分が発
生して塗膜品質を著しく損なうことが知られてい
る。 Here, a direct heating type drying oven has the advantage that it has very good thermal efficiency and can quickly raise the temperature inside the oven because there is no heat loss due to heat exchange and combustion gas is directly introduced into the oven. On the other hand, there is a drawback that dust, impurities, etc. contained in the combustion gas adversely affect the product quality of the object to be coated. In particular, it is known that when petroleum-based fuel is used, sulfur content is generated, which significantly impairs the quality of the coating film.
そこで、厳しい製品品質が要求される自動車塗
装の上塗り乾燥を行う直接加熱式の焼付乾燥炉に
あつては、従来から硫黄分等の不純物が少ない都
市ガスやLPガス等の比較的クリーンな燃料を使
用することとしている。 Therefore, in the case of direct-heating drying ovens for drying top coats of automobile paint, which require strict product quality, relatively clean fuels such as city gas and LP gas, which have low impurities such as sulfur content, have traditionally been used. I plan to use it.
然しながら、本発明者らの実験及び研究によれ
ば、このように燃焼ガスを直接炉内に供給する直
接加熱式乾燥炉によつて自動車ボデイの焼付乾燥
を行う際には、自動車ボデイが120〜200℃(通常
は、150〜160℃)程度の高温で加熱されるから、
塗料に含まれたシンナー、トルエン等の有機溶剤
や塗料樹脂の硬化剤などのアミン化合物等が塗膜
から蒸発し、これらがバーナの火炎に直接接触し
て熱分解され、燃焼生成物の水、窒素酸化物
(NOx成分)のうちラジカルなものと反応するこ
とにより、低分子量樹脂の析出物を主成分とする
脂状物質が生成され、これが自動車ボデイの表面
に付着して塗膜の黄変や層間剥離現象等の弊害を
発生させることが判明した。 However, according to the experiments and research conducted by the present inventors, when baking and drying an automobile body using a direct heating type drying oven that directly supplies combustion gas into the oven, the automobile body Because it is heated at a high temperature of around 200℃ (usually 150-160℃),
Organic solvents such as thinner and toluene contained in the paint, and amine compounds such as hardeners for paint resins, etc., evaporate from the paint film, and these are thermally decomposed by direct contact with the burner flame, resulting in combustion products such as water and By reacting with radical nitrogen oxides (NOx components), a greasy substance whose main component is precipitates of low molecular weight resin is produced, which adheres to the surface of the car body and causes yellowing of the paint film. It has been found that this causes problems such as delamination and delamination.
したがつて、このような直接加熱式特有の弊害
を防止するためには、できるだけ空気比の大きい
バーナを使用するか、あるいは炉内への新鮮空気
の供給量と炉内の汚染空気の排気量とを増大させ
て脂状物質生成の原因物質となる蒸発有機溶剤等
の炉内濃度を低下させなければならず、そのため
のランニングコストが著しく嵩むという重大な欠
点を有していた。 Therefore, in order to prevent these disadvantages specific to direct heating, it is necessary to use a burner with as large an air ratio as possible, or to reduce the amount of fresh air supplied to the furnace and the amount of contaminated air exhausted from the furnace. It is necessary to reduce the concentration in the furnace of evaporated organic solvents, etc., which are the causative substances for the production of greasy substances, and this has a serious disadvantage in that the running cost for this purpose increases significantly.
一方、間接加熱式の乾燥炉は、燃料の燃焼によ
つて発生する塵埃、不純物等を完全に遮断するこ
とができ、前記の如き脂状物質の生成による弊害
も生じないという長所があり、この点では自動車
ボデイ等の仕上げ乾燥に好適であるが、直接加熱
式の乾燥炉に比較して温度上昇率が極めて悪く炉
内の予熱に長時間を要するという欠点を有してい
た。塗装用乾燥炉はなるべく短時間に所定温度ま
で昇温させることが特に重要とされているから、
これは極めて重大な欠点であつた。 On the other hand, indirect heating type drying ovens have the advantage of being able to completely block out dust, impurities, etc. generated by the combustion of fuel, and not causing the harmful effects of producing greasy substances as described above. In this respect, it is suitable for finishing drying automobile bodies, etc., but it has the disadvantage that the rate of temperature rise is extremely slow compared to direct heating type drying ovens, and it takes a long time to preheat the inside of the oven. It is especially important for paint drying ovens to raise the temperature to a specified temperature in as short a time as possible.
This was an extremely serious drawback.
そこで本願発明は、炉内を予熱する昇温時にお
いては直接加熱式乾燥炉の如く炉内に燃焼ガスを
直接循環対流させて短時間で所定温度にまで加熱
することができると共に、炉内が所定温度にまで
達して被塗物が搬入される際には間接加熱式乾燥
炉の如く燃焼ガスとの熱交換によつて加熱された
熱空気を循環対流させて塗膜の黄変や層間剥離の
発生原因となる脂状物質が生成されることなく炉
内を加熱できる塗装用乾燥炉及びその加熱方法を
提供することを目的とする。
Therefore, the present invention makes it possible to heat the inside of the furnace to a predetermined temperature in a short time by directly circulating and convecting the combustion gas inside the furnace like in a direct heating drying furnace when the temperature is raised to preheat the inside of the furnace. When the object to be coated reaches a predetermined temperature and is brought in, hot air heated by heat exchange with combustion gas is circulated and convected in an indirect heating drying oven to prevent yellowing of the coating film and delamination. It is an object of the present invention to provide a coating drying oven and a heating method thereof that can heat the interior of the oven without producing greasy substances that cause the occurrence of oily substances.
この目的を達成するために、本発明は、炉内の
空気を吸引するリターンダクトと熱源から発生す
る燃焼ガスを炉内に導入するサプライダクトが連
通して直接加熱式の熱風循環径路が形成される塗
装用乾燥炉において、前記リターンダクトとサプ
ライダクトに、その各通路を途中で遮断して夫々
の通路を前段側と後段側とに分断できる通路開閉
手段が設けられ、当該両通路開閉手段を前後から
挟むようにしてリターンダクトとサプライダクト
との間に二つの分岐ダクトが並列に接続されると
共に、当該分岐ダクト間に燃焼ガス−空気熱交換
器が介装され、直接加熱式の熱風循環径路を形成
するリターンダクトとサプライダクトの両通路を
前記通路開閉手段で遮断すると共に、前記各分岐
ダクトの両通路を開けることによつて、前記熱源
から発生する燃焼ガスを前記熱交換器を経由して
循環させる閉路と、炉内から吸引した空気を前記
熱交換器に送り込んで前記閉路内を循環する燃焼
ガスから熱の給与を受けさせて再び炉内に導入す
る間接加熱式の熱風循環径路が形成されるように
構成されていることを特徴とする。
In order to achieve this objective, the present invention has a structure in which a return duct that sucks air in the furnace and a supply duct that introduces combustion gas generated from a heat source into the furnace communicate with each other to form a direct heating type hot air circulation path. In the drying oven for painting, the return duct and the supply duct are provided with a passage opening/closing means that can block each passage in the middle and divide each passage into a front stage side and a rear stage side, and the passage opening/closing means can open and close both passages. Two branch ducts are connected in parallel between the return duct and the supply duct so as to sandwich them from the front and back, and a combustion gas-air heat exchanger is interposed between the branch ducts to provide a direct heating type hot air circulation path. By blocking both passages of the return duct and supply duct to be formed by the passage opening/closing means and opening both passages of each branch duct, the combustion gas generated from the heat source is passed through the heat exchanger. A closed circuit for circulation and an indirect heating type hot air circulation path are formed in which air sucked from inside the furnace is sent to the heat exchanger, receives heat from the combustion gas circulating in the closed circuit, and is introduced into the furnace again. It is characterized by being configured so that
本願発明による塗装用乾燥炉は、炉内を予熱す
る昇温時においてリターンダクトとサプライダク
トとを連通させて直接加熱式の熱風循環径路を形
成し、熱源から発生する燃焼ガスを炉内に直接循
環対流させて速やかに所定温度にまで加熱するこ
とができると共に、炉内に被塗物を搬入する際に
おいてリターンダクト及びサプライダクトの通路
を途中で二つに分断させて間接加熱式の熱風循環
径路を形成し、前記燃焼ガスとの熱交換によつて
加熱された熱空気を炉内に循環対流させることが
できる。
The paint drying oven according to the present invention connects the return duct and the supply duct to form a direct heating type hot air circulation path when the temperature rises to preheat the interior of the oven, and directs the combustion gas generated from the heat source into the oven. It is possible to quickly heat up to a predetermined temperature by circulating convection, and when carrying the workpiece into the furnace, the passage of the return duct and supply duct is divided into two in the middle, allowing indirect heating type hot air circulation. By forming a path, hot air heated by heat exchange with the combustion gas can be circulated and convected in the furnace.
また、本願発明による塗装用乾燥炉の加熱方法
は、炉内を予熱する昇温時においては熱源から発
生する燃焼ガスを炉内に循環対流させて直接加熱
することとしているから、炉内が短時間で所定温
度にまで加熱される。また、炉内が所定温度に達
して被塗物が搬入される際には前記燃焼ガスを炉
内に導入していた通路を断つて該燃焼ガスを熱交
換器を経由して循環させると共に、該熱交換器で
前記燃焼ガスから熱の給与を受けた熱空気を炉内
に循環対流させて間接加熱することとしているか
ら、塗膜の黄変や層間剥離の発生原因となる脂状
物質の生成が防止される。 In addition, the heating method for the coating drying oven according to the present invention is such that when the temperature inside the oven is preheated, the combustion gas generated from the heat source is circulated and convected inside the oven for direct heating. It is heated to a predetermined temperature within a certain period of time. Further, when the inside of the furnace reaches a predetermined temperature and the object to be coated is carried in, the passage through which the combustion gas was introduced into the furnace is cut off, and the combustion gas is circulated via a heat exchanger, Since hot air that has received heat from the combustion gas in the heat exchanger is circulated and convected in the furnace for indirect heating, it is possible to eliminate greasy substances that cause yellowing and delamination of the paint film. Generation is prevented.
以下、本願発明を図面に示す具体的な実施例に
基づいて説明する。
Hereinafter, the present invention will be described based on specific embodiments shown in the drawings.
図は本願発明による塗装用乾燥炉及びその加熱
方法の一例を説明するために示すフローシート図
である。 The figure is a flow sheet diagram shown to explain an example of a coating drying oven and a heating method thereof according to the present invention.
図中、1は自動車塗装等の焼付乾燥を行う塗装
用乾燥炉であつて、平型炉あるいは山型炉等の如
く両端が開放されてトンネル形に形成された炉体
2内に自動車ボデイ等の被塗物3が所定速度で連
続的に移送されるように成されている。 In the figure, reference numeral 1 denotes a paint drying furnace for baking and drying automobile paint, etc., and the furnace body 2 is open at both ends and formed in a tunnel shape, such as a flat furnace or a mountain-shaped furnace. The object to be coated 3 is continuously transported at a predetermined speed.
4は炉内空気を吸引するリターンダクト、5は
炉内に熱風を導入するサプライダクトであり、リ
ターンダクト4及びサプライダクト5が連通され
てバーナ6の燃焼ガスを直接炉内に循環対流させ
る直接加熱式の熱風循環径路N1が形成されるよ
うに成されている。 Reference numeral 4 indicates a return duct that sucks air in the furnace, and reference numeral 5 indicates a supply duct that introduces hot air into the furnace. A heated hot air circulation path N1 is formed.
リターンダクト4及びサプライダクト5には、
夫々その通路の途中に風量調整又は通路の遮断を
行う通路開閉手段としてのダンパ7及び8が介装
されると共に、リターンダクト4及びサプライダ
クト5間に前記ダンパ7及び8を挟んで二つの分
岐ダクト9及び10が並列に接続され、これら分
岐ダクト9及び10間に燃焼ガス−空気熱交換器
11が介装されて、前記ダンパ7及び8を閉じて
リターンダクト4及びサプライダクト5の通路を
夫々二つに分断させることによりバーナ6から発
生する燃焼ガスを分岐ダクト9から熱交換器11
を経由して循環させる閉路Gと、リターンダクト
4から吸引される炉内空気を分岐ダクト10から
熱交換器11に送り込み前記燃焼ガスから熱の給
与を受けさせた後に炉内に導入させる間接加熱式
の熱風循環径路N2が形成されるように成されて
いる。 The return duct 4 and supply duct 5 include
Dampers 7 and 8 as passage opening/closing means for adjusting the air volume or blocking the passage are interposed in the middle of each passage, and two branches are provided between the return duct 4 and the supply duct 5 with the dampers 7 and 8 sandwiched between them. Ducts 9 and 10 are connected in parallel, and a combustion gas-air heat exchanger 11 is interposed between these branch ducts 9 and 10, closing the dampers 7 and 8 to open the passages of the return duct 4 and supply duct 5. By dividing each burner into two, the combustion gas generated from the burner 6 is transferred from the branch duct 9 to the heat exchanger 11.
indirect heating in which the furnace air sucked from the return duct 4 is sent into the heat exchanger 11 from the branch duct 10 to receive heat from the combustion gas, and then introduced into the furnace. A hot air circulation path N2 of the formula is formed.
閉路Gには、ブロアー12から燃焼用空気が供
給されるバーナ6のほかに循環フアン13が介装
され、バーナ6から発生せられた燃焼ガスが循環
フアン13によつて分岐ダクト9を通じて熱交換
器11のエロフインチユーブ内に送られ、該エロ
フインチユーブのフイン等から効果的に放熱した
後、再びバーナ6で加熱されて循環せられるよう
に成されている。また、分岐ダクト9には熱交換
器11を挟んで二つのダンパ14及び15が介装
されて、該分岐ダクト9の通路を開閉するように
成されている。 In addition to the burner 6 to which combustion air is supplied from the blower 12, a circulation fan 13 is installed in the closed circuit G, and the combustion gas generated from the burner 6 is heat exchanged by the circulation fan 13 through the branch duct 9. After being sent into the erofinche tube of the container 11 and effectively dissipating heat from the fins of the fins, etc., it is heated again by the burner 6 and circulated. Further, two dampers 14 and 15 are interposed in the branch duct 9 with a heat exchanger 11 in between, so as to open and close the passage of the branch duct 9.
熱風循環径路N2には、リターンダクト4側に
フイルタ16が介装されると共に、サプライダク
ト5側に循環フアン17が介装され、該循環フア
ン17によりリターンダクト4から炉内空気が吸
引されて、分岐ダクト10に介装された熱交換器
11に送られ、該熱交換器11内のエロフインチ
ユーブ間を通つて加熱された後、サプライダクト
5を通つて炉内に循環対流せられるように成され
ている。また、分岐ダクト10には熱交換器11
を挟んで二つのダンパ18及び19が介装され、
エロフインチユーブ間を通過する空気の流速を最
適値(例えば、4m/sec程度)に調整すると共
に、該分岐ダクト10の通路を開閉するように成
されている。 In the hot air circulation path N2, a filter 16 is installed on the return duct 4 side, and a circulation fan 17 is installed on the supply duct 5 side, and the furnace air is sucked from the return duct 4 by the circulation fan 17. , is sent to the heat exchanger 11 installed in the branch duct 10, is heated through the air-finches in the heat exchanger 11, and is then circulated and convected into the furnace through the supply duct 5. has been made. In addition, a heat exchanger 11 is provided in the branch duct 10.
Two dampers 18 and 19 are interposed between them,
The flow rate of air passing between the air-finches is adjusted to an optimum value (for example, about 4 m/sec), and the passage of the branch duct 10 is opened and closed.
なお、図示は省略するが、前記各ダンパは炉内
に配設された温度安全リミツトスイツチや温度制
御ポテンシヨンメータ等から発せられる操作信号
に従つて作動するシリンダ若しくはモジユトルモ
ータ等によつて自動的に開閉制御されるように成
されている。 Although not shown, each damper is automatically opened and closed by a cylinder or module motor, etc., which operates in accordance with an operation signal issued from a temperature safety limit switch, temperature control potentiometer, etc. installed in the furnace. It is made to be controlled.
以上が本願発明による塗装用乾燥炉の一例構成
であり、次にその作用及び本願発明による塗装用
乾燥炉の具体的な加熱方法について説明する。 The above is an example of the structure of the coating drying oven according to the present invention, and next, its operation and a specific heating method of the coating drying oven according to the present invention will be explained.
まず、乾燥炉の運転を開始して炉内を予熱する
昇温時においては、分岐ダクト9に介装されたダ
ンパ14及び15を完全に閉じ、分岐ダクト10
に介装されたダンパ18及び19を極く僅か開い
た状態にして、リターンダクト4及びサプライダ
クト5に介装されたダンパ7及び8を開き、バー
ナ6及び循環フアン13及び17を稼働させて、
リターンダクト4から吸引された炉内空気をバー
ナ6から発生する燃焼ガスで例えば300℃程度の
高温に加熱し、該燃焼ガスと共にサプライダクト
5を通じて炉内に循環対流させる直接加熱式の熱
風循環径路N1を形成し、炉内を速やかに所定温
度にまで加熱する。 First, when the drying oven starts operating and the temperature rises to preheat the inside of the oven, the dampers 14 and 15 installed in the branch duct 9 are completely closed, and the branch duct 10
The dampers 18 and 19 installed in the return duct 4 and the supply duct 5 are opened, and the burner 6 and circulation fans 13 and 17 are operated. ,
A direct heating type hot air circulation path in which the air in the furnace sucked through the return duct 4 is heated to a high temperature of, for example, about 300°C with the combustion gas generated from the burner 6, and is circulated and convected into the furnace together with the combustion gas through the supply duct 5. N1 is formed, and the inside of the furnace is quickly heated to a predetermined temperature.
これにより、炉内が所定温度(例えば、150〜
160℃程度)に達すると、自動的にダンパ7及び
8が全閉されてリターンダクト4及びサプライダ
クト5の通路が二つに分断されると共に、分岐ダ
クト9及び10に介装された各ダンパ14,15
及び18,19が所要開度で開かれて、それまで
の熱風循環径路N1に代わつて閉路Gと間接加熱
式の熱風循環径路N2が形成されることとなる。
即ち、乾燥炉1が自動的に直接加熱式から間接加
熱式に切り替えられ、閉路Gではバーナ6の燃焼
ガスが循環フアン13により熱交換器11を経由
して循環されると共に、その一部が閉路Gに連結
された排気ダクト20を通じて外部に排出され、
また熱風循環径路N2では循環フアン17により
リターンダクト4から吸引された温度150℃前後
の炉内空気が熱交換器11に送り込まれて燃焼ガ
スから熱の給与を受けて例えば170℃程度に加熱
された後、サプライダクト5から炉内に循環対流
せられる。なお、上記の如く熱風循環径路N1を
形成して直接加熱を行う際に、分岐ダクト10に
介装されたダンパ18及び19を完全に閉じずに
僅かに開いて少量の熱風が流通するようにしてお
けば、熱風循環径路N2への切り替え初期時に分
岐ダクト10内に滞留していた低温の空気が炉内
に導入されて一時的に炉内温度が低下することが
ないという利点がある。 This allows the inside of the furnace to reach a predetermined temperature (for example, 150~
When the temperature reaches approximately 160°C), the dampers 7 and 8 are automatically fully closed and the passages of the return duct 4 and supply duct 5 are divided into two, and each damper installed in the branch ducts 9 and 10 is closed. 14,15
, 18 and 19 are opened at the required opening degree, and a closed path G and an indirect heating type hot air circulation path N2 are formed in place of the hot air circulation path N1.
That is, the drying oven 1 is automatically switched from the direct heating type to the indirect heating type, and in the closed circuit G, the combustion gas of the burner 6 is circulated by the circulation fan 13 via the heat exchanger 11, and a part of it is Exhausted to the outside through an exhaust duct 20 connected to the closed circuit G,
Further, in the hot air circulation path N2, the furnace air at a temperature of around 150°C is sucked from the return duct 4 by the circulation fan 17 and is sent to the heat exchanger 11, where it receives heat from the combustion gas and is heated to, for example, about 170°C. After that, it is circulated and convected from the supply duct 5 into the furnace. In addition, when forming the hot air circulation path N1 and performing direct heating as described above, the dampers 18 and 19 installed in the branch duct 10 are not completely closed but are slightly opened to allow a small amount of hot air to flow. If this is done, there is an advantage that the low-temperature air stagnant in the branch duct 10 at the initial stage of switching to the hot air circulation path N2 will not be introduced into the furnace and the temperature in the furnace will not temporarily drop.
そして、このように乾燥炉1が間接加熱式に切
り替えられてから炉体2内に上塗り塗装が施され
た自動車ボデイ等の被塗物3を搬入して移送させ
る。これにより、被塗物3が高温で加熱されてそ
の塗膜から有機溶剤や硬化剤のアミン化合物等が
蒸発するが、これらはバーナ6の火炎に接触され
ることがないから塗膜の黄変や層間剥離の原因と
なる脂状物質の生成が防止され、製品品質を良好
に維持することができる。 After the drying oven 1 is switched to the indirect heating type in this way, the article 3 to be coated, such as an automobile body, which has been topcoated, is brought into the oven body 2 and transported. As a result, the object to be coated 3 is heated to a high temperature, and the organic solvent and the amine compound of the hardening agent evaporate from the coating film, but since these are not brought into contact with the flame of the burner 6, the coating film yellows. This prevents the production of greasy substances that cause delamination and delamination, and maintains good product quality.
以上述べたように、本願発明によれば、炉内を
予熱する昇温時においてはバーナ等の熱源から発
生する燃焼ガスを直接炉内に循環対流させて炉内
温度を短時間で上昇させることができると同時
に、炉内が所定温度に達して被塗物を搬入する際
においては前記燃焼ガスとの熱交換によつて加熱
される熱空気を炉内に循環対流させて塗膜の黄変
や層間剥離の原因となる脂状物質の生成を防止す
ることができるという優れた効果がある。
As described above, according to the present invention, when raising the temperature to preheat the inside of the furnace, combustion gas generated from a heat source such as a burner is circulated directly into the furnace to raise the temperature inside the furnace in a short time. At the same time, when the inside of the furnace reaches a predetermined temperature and the object to be coated is brought in, hot air heated by heat exchange with the combustion gas is circulated and convected inside the furnace to prevent yellowing of the coating film. It has the excellent effect of preventing the formation of greasy substances that cause delamination and delamination.
また、従来の直接加熱式乾燥炉に比較すると、
脂状物質生成の原因物質である有機溶剤等の濃度
を低下させるために空気比の大きいバーナを使用
したり、あるいは新鮮空気を給気し汚染空気を排
気させる大掛りな装置を使用する必要がなく、ラ
ンニングコストが大幅に低減されるという効果も
ある。 Also, compared to conventional direct heating drying ovens,
It is necessary to use a burner with a large air ratio to reduce the concentration of organic solvents, etc. that cause the production of greasy substances, or to use large-scale equipment that supplies fresh air and exhausts contaminated air. This also has the effect of significantly reducing running costs.
図は、本願発明による塗装用乾燥炉及びその加
熱方法の一例を説明するために示すフローシート
図である。
符号の説明、1……塗装用乾燥炉、2……炉
体、3……被塗物、4……リターンダクト、5…
…サプライダクト、6……バーナ(熱源)、7,
8……ダンパ、9,10……分岐ダクト、11…
…燃焼ガス−空気熱交換器、13……循環フア
ン、14,15……ダンパ、17……循環フア
ン、18,19……ダンパ、N1……直接加熱式
の熱風循環径路、N2……間接加熱式の熱風循環
径路、G……閉路。
The figure is a flow sheet diagram shown to explain an example of a coating drying oven and a heating method thereof according to the present invention. Explanation of symbols, 1... Painting drying oven, 2... Furnace body, 3... Subject to be coated, 4... Return duct, 5...
...Supply duct, 6...Burner (heat source), 7,
8... Damper, 9, 10... Branch duct, 11...
... Combustion gas-air heat exchanger, 13 ... Circulation fan, 14, 15 ... Damper, 17 ... Circulation fan, 18, 19 ... Damper, N1 ... Direct heating type hot air circulation path, N2 ... Indirect Heated hot air circulation path, G...closed circuit.
Claims (1)
源6から発生する燃焼ガスを炉内に導入するサプ
ライダクト5が連通して直接加熱式の熱風循環径
路N1が形成される塗装用乾燥炉において、前記
リターンダクト4とサプライダクト5に、その各
通路を途中で遮断して夫々の通路を前段側と後段
側とに分断できる通路開閉手段7,8が設けら
れ、当該両通路開閉手段7,8を前後から挟むよ
うにしてリターンダクト4とサプライダクト5と
の間に二つの分岐ダクト9,10が並列に接続さ
れると共に、当該分岐ダクト9,10間に燃焼ガ
ス−空気熱交換器11が介装され、直接加熱式の
熱風循環径路N1を形成するリターンダクト4と
サプライダクト5の両通路を前記通路開閉手段
7,8で遮断すると共に、前記各分岐ダクト9,
10の両通路を開けることによつて、前記熱源6
から発生する燃焼ガスを前記熱交換器11を経由
して循環させる閉路Gと、炉内から吸引した空気
を前記熱交換器11に送り込んで前記閉路G内を
循環する燃焼ガスから熱の給与を受けさせて再び
炉内に導入する間接加熱式の熱風循環径路N2が
形成されるように構成されていることを特徴とす
る塗装用乾燥炉。 2 炉内を予熱する昇温時においては、その炉内
の空気を吸引するリターンダクト4と熱源6から
発生する燃焼ガスを炉内に導入するサプライダク
ト5とを連通させて直接加熱式の熱風循環径路
N1を形成し、当該熱風循環径路N1を通じて前記
燃焼ガスを直接炉内に循環対流させ、その燃焼ガ
スの循環対流によつて炉内が所定の温度に達した
時には、前記リターンダクト4とサプライダクト
5の各通路を途中で遮断して夫々の通路を前段側
と後段側とに分断すると共に、その分断箇所を挟
むようにして前記リターンダクト4とサプライダ
クト5との間に並列に接続された二つの分岐ダク
ト9,10の両通路を開けて、当該両分岐ダクト
9,10間に介装された燃焼ガス−空気熱交換器
11を経由して前記燃焼ガスを循環させる閉路G
と、炉内から吸引した空気を前記熱交換器11に
送り込んで再び炉内に導入させる間接加熱式の熱
風循環径路N2を形成し、当該熱風循環径路N2を
通じて前記閉路G内を循環する燃焼ガスとの熱交
換によつて加熱された熱空気を炉内に循環対流さ
せるようにしたことを特徴とする塗装用乾燥炉の
加熱方法。[Claims] 1. A return duct 4 that sucks air in the furnace and a supply duct 5 that introduces combustion gas generated from a heat source 6 into the furnace communicate with each other to form a direct heating type hot air circulation path N1 . In the drying oven for painting, the return duct 4 and the supply duct 5 are provided with passage opening/closing means 7 and 8 that can block each passage in the middle and divide each passage into a front stage side and a rear stage side. Two branch ducts 9 and 10 are connected in parallel between the return duct 4 and the supply duct 5 so as to sandwich the passage opening/closing means 7 and 8 from the front and back, and between the branch ducts 9 and 10, combustion gas and air are A heat exchanger 11 is interposed between the return duct 4 and the supply duct 5 , which form a direct heating type hot air circulation path N1, and the passage opening/closing means 7 and 8 block off both passages, and each of the branch ducts 9,
By opening both passages of 10, the heat source 6
A closed circuit G circulates combustion gas generated from the furnace via the heat exchanger 11, and air sucked from inside the furnace is sent to the heat exchanger 11 to receive heat from the combustion gas circulating in the closed circuit G. A painting drying oven characterized in that it is configured to form an indirect heating type hot air circulation path N2 for receiving the hot air and introducing it into the oven again. 2. When raising the temperature to preheat the inside of the furnace, the return duct 4 that sucks the air inside the furnace and the supply duct 5 that introduces the combustion gas generated from the heat source 6 into the furnace are connected to directly heat hot air. circulation path
The combustion gas is directly circulated and convected into the furnace through the hot air circulation path N1 , and when the inside of the furnace reaches a predetermined temperature due to the circulation convection of the combustion gas, the return duct 4 and Each passage of the supply duct 5 is blocked in the middle to divide each passage into a front stage side and a rear stage side, and is connected in parallel between the return duct 4 and the supply duct 5 so as to sandwich the divided part. A closed circuit G in which both passages of the two branch ducts 9 and 10 are opened and the combustion gas is circulated via the combustion gas-air heat exchanger 11 interposed between the two branch ducts 9 and 10.
Then, an indirect heating type hot air circulation path N2 is formed in which the air sucked from inside the furnace is sent to the heat exchanger 11 and introduced into the furnace again, and the air is circulated in the closed circuit G through the hot air circulation path N2 . A method for heating a paint drying furnace, characterized in that hot air heated by heat exchange with combustion gas is circulated and convected within the furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP222585A JPS61161173A (en) | 1985-01-11 | 1985-01-11 | Drying furnace for painting and heating method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP222585A JPS61161173A (en) | 1985-01-11 | 1985-01-11 | Drying furnace for painting and heating method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61161173A JPS61161173A (en) | 1986-07-21 |
JPH0333386B2 true JPH0333386B2 (en) | 1991-05-16 |
Family
ID=11523410
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP222585A Granted JPS61161173A (en) | 1985-01-11 | 1985-01-11 | Drying furnace for painting and heating method thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61161173A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3251157B2 (en) * | 1995-10-03 | 2002-01-28 | 株式会社大氣社 | Paint drying oven |
JP3133659B2 (en) * | 1995-10-04 | 2001-02-13 | 株式会社大氣社 | Paint drying oven |
-
1985
- 1985-01-11 JP JP222585A patent/JPS61161173A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS61161173A (en) | 1986-07-21 |
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