JPH0461953A - Coat drying furnace - Google Patents

Coat drying furnace

Info

Publication number
JPH0461953A
JPH0461953A JP16964390A JP16964390A JPH0461953A JP H0461953 A JPH0461953 A JP H0461953A JP 16964390 A JP16964390 A JP 16964390A JP 16964390 A JP16964390 A JP 16964390A JP H0461953 A JPH0461953 A JP H0461953A
Authority
JP
Japan
Prior art keywords
furnace
temperature
combustion
combustion device
air
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
JP16964390A
Other languages
Japanese (ja)
Other versions
JP3043372B2 (en
Inventor
Kazuaki Toyoshima
豊島 和昭
Etsuo Kawahara
河原 悦男
Tadahiko Imamura
今村 忠彦
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.)
Taikisha Ltd
Suzuki Motor Corp
Original Assignee
Taikisha Ltd
Suzuki Motor Corp
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 Taikisha Ltd, Suzuki Motor Corp filed Critical Taikisha Ltd
Priority to JP2169643A priority Critical patent/JP3043372B2/en
Publication of JPH0461953A publication Critical patent/JPH0461953A/en
Application granted granted Critical
Publication of JP3043372B2 publication Critical patent/JP3043372B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Coating Apparatus (AREA)
  • Tunnel Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

PURPOSE:To make the operation of a coat drying furnace stable and solve the problems arising from energy conservation by a method wherein the amt. of exhaust air supplied into a combustion device and the amt. of a fresh air supplied to a convection hot air by an air supply means are controlled according to the number of the coated objects in a furnace. CONSTITUTION:A control device 10 computes the number of coated objects A in a furnace 20 using the detection signals supplied by sensors 11 and 12 to the control device and, if the resulting value is O, it reduces the combustion temp. of a combustion device 30 from a predetermined temp. suitable for incinerating treatment to such a value as not to hinder the maintenance of the temp. inside the furnace and also functions as a temp. setting means 50 which brings the combustion temp. of the combustion device 30 when the introduction of the objects A into the furnace is expected back to a predetermined temp. The combustion temp. of the combustion device 30 is regulated by adjusting a burner 30a provided in the combustion device 30.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は塗装物を加熱乾燥する塗装乾燥炉に関し、詳し
くは、炉体内の塗装物を対流熱風によって加熱乾燥する
ときに発生する溶剤ガスを含む排気空気が供給され、該
排気空気を燃焼させて焼却処理した上て高温燃焼排ガス
として排出する燃焼装置を備え、該燃焼装置からの高温
燃焼排ガスと熱交換させて加熱したフレッシュエアを炉
内温度維持用に前記対流熱風に補給するエア供給手段を
備えた塗装乾燥炉に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention relates to a paint drying furnace for heating and drying painted objects, and more specifically, the present invention relates to a paint drying furnace that heats and dries painted objects. The furnace is equipped with a combustion device that is supplied with exhaust air containing carbon dioxide, burns the exhaust air, incinerates it, and then discharges it as high-temperature combustion exhaust gas. The present invention relates to a paint drying oven equipped with an air supply means for replenishing the convective hot air for temperature maintenance.

〔従来の技術〕[Conventional technology]

かかる塗装乾燥炉は、例えば第2図に示すように、炉体
(20)内の塗装物(A)を対流熱風によって加熱乾燥
するものであり、該塗装乾燥炉には、燃焼装置(30)
及びエア供給手段(40)か設げられている。
As shown in FIG. 2, for example, such a paint drying furnace heat-dries the painted object (A) in a furnace body (20) using convection hot air, and the paint drying furnace is equipped with a combustion device (30).
and air supply means (40).

前記燃焼装置(30)には炉内の塗装物(A)の加熱乾
燥に伴って発生する溶剤ガスを含む炉内からの排気かダ
クト(26)を介して供給される。該燃焼装置(30)
においては、前記排気が所定温度て燃焼焼却処理された
後、高温燃焼排ガスとしてダクト(32)へ排出される
The combustion device (30) is supplied with exhaust gas from the furnace containing a solvent gas generated as the coated article (A) in the furnace is heated and dried through a duct (26). The combustion device (30)
After the exhaust gas is incinerated at a predetermined temperature, it is discharged into the duct (32) as high-temperature combustion exhaust gas.

前記燃焼装置(30)から排出される高温燃焼排ガスは
、熱交換器(41)を備える前記エア供給手段(40)
へ供給される。該エア供給手段(40)においては、外
気からフレッシュエア供給管(43)を介して取り入れ
られるフレッシュエアが前記高温燃焼排ガスと熱交換さ
れて加熱される。そして、その加熱されたフレッシュエ
アは炉内へ補給される。
The high temperature combustion exhaust gas discharged from the combustion device (30) is supplied to the air supply means (40) including a heat exchanger (41).
supplied to In the air supply means (40), fresh air taken in from the outside air via the fresh air supply pipe (43) is heated by exchanging heat with the high temperature combustion exhaust gas. The heated fresh air is then supplied into the furnace.

かかる塗装乾燥炉においては、燃焼装置(30)で焼却
処理される前記排気の量(以下、単に排気量という)と
、エア供給手段(40)にて炉内へ補給されるフレッシ
ュエアの補給量(以下、単に補給量という)とを等しい
Iとして、炉内の風量需給バランスか保たれるか、従来
、前記排気量と前記補給量とは、炉内における塗装物(
A)の数量変動に拘らず一定とされていた。
In such a paint drying furnace, the amount of the exhaust gas that is incinerated by the combustion device (30) (hereinafter simply referred to as exhaust amount) and the amount of fresh air supplied to the furnace by the air supply means (40) are determined. (hereinafter simply referred to as replenishment amount) is equal to I, and whether the air volume supply and demand balance in the furnace can be maintained. Conventionally, the displacement amount and the replenishment amount are
A) was assumed to be constant regardless of changes in quantity.

そして、炉内の温度調整については、燃焼装置(30)
からの高温燃焼排ガスと外気から取り入れられるフレッ
シュエアとの熱交換量を調整(具体的には、熱交換器(
41)をバイパスさせるフレッシュエアの量をバイパス
ダンパ(42)によって調整)することにより、塗装物
(A)の数量変動(即ち炉内負荷変動)に拘らず、炉内
温度を塗装物乾燥に適した温度に保つようにしていた。
And for temperature adjustment inside the furnace, the combustion device (30)
Adjust the amount of heat exchange between the high-temperature combustion exhaust gas from the outside and the fresh air taken in from the outside air (specifically,
41) by adjusting the amount of fresh air bypassed by the bypass damper (42)), the temperature inside the furnace can be adjusted to suit the drying of the painted objects, regardless of changes in the quantity of painted objects (A) (i.e., fluctuations in the load inside the furnace). I tried to keep it at a certain temperature.

つまり、前記塗装乾燥炉においては、炉内からの排気に
含まれる溶剤ガス等を焼却処理する上で燃焼装置(30
)の燃焼温度は所定温度に維持しなければならない制約
があることから、前記排気量と前記補給量とか一定であ
る条件下で、塗装物(A)の数量変動に応じて、前記高
温燃焼排ガスと前記フレッシュエアとの熱交換量(高温
燃焼排ガスからフレッシュエアに付与する熱量)を調整
することにより、炉内への補給熱量を調整し、炉内温度
を適切温度に維持するようにしていた。
In other words, in the paint drying furnace, the combustion device (30
) has to be maintained at a predetermined temperature. Therefore, under the condition that the exhaust volume and the replenishment amount are constant, the high temperature combustion exhaust gas is By adjusting the amount of heat exchange between the fresh air and the fresh air (the amount of heat given to the fresh air from the high-temperature combustion exhaust gas), the amount of heat supplied to the furnace was adjusted, and the temperature inside the furnace was maintained at an appropriate temperature. .

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

かかる従来の塗装乾燥炉においては、前記排気量か一定
であり、且つ、燃焼装置(30)の燃焼温度か一定であ
るため、燃焼装置(3o)からの高温燃焼排ガスの保有
熱量か常に一定となる。そこて、炉内の塗装物(A)の
数量が少量となって前記高温燃焼排ガスと前記フレッシ
ュエアとの熱交換量が少量に調整されると、フレッシュ
エアの加熱に寄与することなく系外へ廃棄される高温燃
焼排ガスの保有熱(以下、系外廃棄熱量という)が大き
くなってエネルギー的に大きな損失が生じるという問題
があった。
In such a conventional paint drying oven, the displacement is constant and the combustion temperature of the combustion device (30) is also constant, so the amount of heat retained in the high-temperature combustion exhaust gas from the combustion device (3o) is always constant. Become. Therefore, when the number of coated objects (A) in the furnace is small and the amount of heat exchange between the high-temperature combustion exhaust gas and the fresh air is adjusted to a small amount, the coating material (A) is removed from the system without contributing to the heating of the fresh air. There has been a problem in that the heat retained in the high-temperature combustion exhaust gas that is disposed of (hereinafter referred to as the amount of heat disposed of outside the system) increases, resulting in a large energy loss.

本発明はかかる事情に鑑みてなされたものであり、塗装
乾燥炉の安定稼働、及び前記排気中の溶剤ガス等の焼却
処理を適切に行いつつ、上述した如き省エネルギー上の
問題を解消し得る塗装乾燥炉を提供することを目的とす
る。
The present invention has been made in view of the above circumstances, and provides a coating that can solve the above-mentioned energy saving problems while ensuring stable operation of the paint drying oven and appropriately incinerating the solvent gas etc. in the exhaust gas. The purpose is to provide a drying oven.

〔課題を解決するための手段〕[Means to solve the problem]

本発明による塗装乾燥炉の第1の特徴構成は、炉体内の
塗装物を対流熱風によって加熱乾燥するときに発生する
溶剤ガスを含む排気空気か供給され、該排気空気を燃焼
させて焼却処理した上で高温燃焼排ガスとして排出する
燃焼装置を備え、 前記燃焼装置からの高温燃焼排ガスと熱交換させて加熱
したフレッシュエアを炉内温度維持用に前記対流熱風へ
補給するエア供給手段を備えた塗装乾燥炉であって、 前記炉内における塗装物の数量に応じて、前記燃焼装置
への排気空気の供給量及び前記エア供給手段によるフレ
ッシュエアの前記対流熱風への補給量を制御する制御手
段を備えることにあり、その作用・効果は次の通りであ
る。
The first characteristic configuration of the paint drying furnace according to the present invention is that exhaust air containing solvent gas generated when a painted object inside the furnace is heated and dried by convection hot air is supplied, and the exhaust air is combusted and incinerated. a combustion device for discharging as high-temperature combustion exhaust gas from the combustion device, and an air supply means for replenishing the convective hot air with fresh air heated by exchanging heat with the high-temperature combustion exhaust gas from the combustion device to maintain the temperature inside the furnace. A drying oven, comprising control means for controlling the amount of exhaust air supplied to the combustion device and the amount of fresh air supplied to the convective hot air by the air supply means according to the number of coated objects in the oven. The purpose is to be prepared, and its functions and effects are as follows.

〔作 用〕[For production]

かかる特徴構成によれば、前記制御手段をもって、炉内
の塗装物の数量が減少するほど、前2排気量及び前記補
給量を互いに同調させて減少させるという制御か行える
According to this characteristic configuration, the control means can perform control such that as the number of coated objects in the furnace decreases, the first two exhaust volumes and the replenishment volume are decreased in synchronization with each other.

かかる制御を行うと、焼却処理上、燃焼装置の燃焼温度
は一定に保つことに対し、前記排気量か炉内の塗装物の
数量の減少に応じて減少させられることで、燃焼装置か
らの高温燃焼排ガスの保有熱量自体か前記塗装物の数量
の減少に応じて減少することになるので、炉内負荷の減
少に対して炉内温度を適切温度に維持すべく炉内への補
給熱量を減少させるのに、系外廃棄熱量の増大が効果的
に回避された状態で系内への補給熱量を減少させること
かできる。
When such control is performed, the combustion temperature of the combustion equipment is kept constant during incineration processing, but it is reduced according to the amount of exhaust gas or the number of coated materials in the furnace, so that the high temperature from the combustion equipment is reduced. Since the amount of heat held by the combustion exhaust gas itself will decrease as the number of coated objects decreases, the amount of heat supplied to the furnace will be reduced in order to maintain the temperature inside the furnace at an appropriate temperature in response to the decrease in the load inside the furnace. However, it is possible to reduce the amount of heat supplied into the system while effectively avoiding an increase in the amount of heat discarded outside the system.

尚、炉内の風量需給バランスは、前記排気量及び前記補
給量の同調減少によって保たれることはいうまでもない
It goes without saying that the air volume supply and demand balance within the furnace is maintained by synchronized reduction of the displacement amount and the replenishment amount.

〔発明の効果〕〔Effect of the invention〕

かくして、本発明によれば、塗装乾燥炉の炉内の風量需
給バランスか保たれることで、塗装乾燥炉の運転が安定
的に行える上、燃焼装置の燃焼温度が所定温度に保たれ
ることで、排気中の溶剤ガス等の焼却処理も適切に行え
ながら、炉内の塗装物の減少時のエネルギー損失を効果
的に回避できることて、塗装乾燥炉における排ガス利用
による所期の省エネルギーか一層効果的に達成されるよ
うになる。
Thus, according to the present invention, by maintaining the air volume supply and demand balance within the paint drying furnace, the paint drying furnace can be operated stably, and the combustion temperature of the combustion device can be maintained at a predetermined temperature. This makes it possible to appropriately incinerate solvent gases etc. in the exhaust gas while effectively avoiding energy loss when the coating material in the furnace decreases, making the intended energy savings by using exhaust gas in the paint drying furnace even more effective. will be achieved.

〔本発明の第2の特徴構成〕 本発明による塗装乾燥炉の第2の特徴構成は、前記塗装
物が前記炉体内に存在しない状態ての前記燃焼装置の燃
焼温度を、前記焼却処理に適した所定温度から、前記炉
内温度維持に支障のない程度まで下げると共に、前記塗
装物の炉内搬入か予期された状態での前記燃焼装置の燃
焼温度を前記所定温度に戻す温度設定手段を備えている
ことにある。
[Second characteristic configuration of the present invention] A second characteristic configuration of the paint drying furnace according to the present invention is such that the combustion temperature of the combustion device in a state where the painted object is not present in the furnace body is set to a temperature suitable for the incineration process. temperature setting means for lowering the combustion temperature of the combustion device from the predetermined temperature to a level that does not interfere with maintaining the temperature in the furnace, and returning the combustion temperature of the combustion device to the predetermined temperature when the painted object is brought into the furnace or in a state expected. It is in the fact that

かかる特徴構成を備える塗装乾燥炉を用いる場合、高温
に設定されてエネルギー消費の大きい前記燃焼装置の燃
焼温度を、塗装物か炉体内に存在しなくて前記排気空気
か出ない状態では、前記温度設定手段によって、前記焼
却処理に適した所定温度から炉内温度維持に支障のない
条件下て下げることかでき、−層の省エネルギー効果か
ある。しかも、前記温度設定手段によれば、前記塗装物
の炉内搬入か予期された状態での前記燃焼装置の燃焼温
度を前記所定温度に戻すことかできるため、塗装乾燥炉
の継続稼働か支障なく行える。
When using a paint drying oven having such a characteristic configuration, the combustion temperature of the combustion device, which is set at a high temperature and consumes a large amount of energy, is lowered to the above temperature when there is no painted object in the furnace body and the exhaust air does not come out. By means of the setting means, the temperature can be lowered from the predetermined temperature suitable for the incineration process under conditions that do not interfere with maintaining the temperature inside the furnace, resulting in an energy saving effect. Moreover, according to the temperature setting means, it is possible to return the combustion temperature of the combustion device to the predetermined temperature when the painted material is brought into the furnace, so that the paint drying furnace can continue to operate without any problem. I can do it.

〔実施例〕〔Example〕

以下、本発明の実施例を図面に基ついて説明する。 Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明に係る塗装乾燥炉の一実施例を示してお
り、図中の(20)はトンネル状の炉体を示している。
FIG. 1 shows an embodiment of a paint drying furnace according to the present invention, and (20) in the figure indicates a tunnel-shaped furnace body.

該炉体(20)内には、塗装物(A)を吊支搬送する搬
送装置(25)が、炉入口(20a)から炉出口(20
b)へわたるように配置されている。そして、該搬送装
置(25)によって塗装物(A)が炉内搬送される間に
、該塗装物(A)には加熱乾燥処理が施されるようにな
っている。
Inside the furnace body (20), a conveying device (25) for conveying the coated article (A) on a suspended support is installed from the furnace inlet (20a) to the furnace outlet (20a).
b). Then, while the coated article (A) is being conveyed into the furnace by the conveying device (25), the coated article (A) is subjected to a heating drying process.

前記炉体(20)内は、前記搬送装置(25)によって
炉体(20)内を搬送される塗装物(A)を対流熱風に
よって加熱し乾燥に適した温度まで昇温させる昇温ゾー
ン(21)と、前記塗装物(、A)を対流熱風によって
恒温保持する恒温ゾーン(22)とに区分けされている
。なお、前記恒温ゾーン(22)は更に、第1恒温ゾー
ン(23)と第2恒温ゾーン(24)との二つのゾーン
に区分けされている。
Inside the furnace body (20), a temperature raising zone ( 21) and a constant temperature zone (22) in which the coated object (A) is maintained at a constant temperature by convection hot air. Note that the constant temperature zone (22) is further divided into two zones: a first constant temperature zone (23) and a second constant temperature zone (24).

前記昇温ゾーン(21)、前記第1恒温ゾーン(23)
、前記第2恒温ゾーン(24)には夫々、ファン(21
a)、 (23a)、 (24a)か中途介装されたダ
クト(21b)、 (23b)、 (24b)の両端か
通気可能状態に接続されており、前記ファン(21a)
、 (23a)、 (24a)の作動により、前記ダク
ト(21b)、 (23b)、 (24b)内に前記各
ゾーン(21)、 (23)、 (24)と通じる循環
風路(2LA)、 (23A)、 (24A)か生じる
ようになっている。そして、該循環風路(21A)、 
(23A)、 (24A)を経路の一部として前記対流
熱風か循環するようになっている。
The temperature increasing zone (21), the first constant temperature zone (23)
, a fan (21) is provided in the second constant temperature zone (24), respectively.
a), (23a), (24a) or both ends of the intermediately inserted ducts (21b), (23b), (24b) are connected to allow ventilation, and the fan (21a)
, (23a), (24a), a circulating air path (2LA) communicating with the zones (21), (23), (24) in the ducts (21b), (23b), (24b); (23A) and (24A) are generated. and the circulation air path (21A),
(23A) and (24A) are used as part of the path to circulate the convective hot air.

前記炉体(20)には、前記塗装物(A)の加熱乾燥に
伴って発生する溶剤ガスやヤニ成分等を含む排気を前記
炉体(20)から排出するためのダクト(26)の一端
が接続されている。該ダクト(26)の他端側は、排気
予熱用熱交換器(31)を経由して燃焼装置(30)に
接続されており、該ダクト(26)によって排気は燃焼
装置(30)へ供給されるようになっている。尚、該ダ
クト(26)による前記排気の燃焼装置(30)への供
給量は、該ダクト(26)に中途介装されているファン
(26a)の制御によって行われる。そして、該燃焼装
置(30)においては、前記ダクト(26)経由で供給
される排気を燃焼させ、該排気中の溶剤ガスやヤニ成分
等の有害成分を焼却処理するようになっている。
The furnace body (20) is provided with one end of a duct (26) for discharging exhaust gas containing solvent gas, tar components, etc. generated during heating and drying of the coated object (A) from the furnace body (20). is connected. The other end of the duct (26) is connected to the combustion device (30) via an exhaust gas preheating heat exchanger (31), and the duct (26) supplies exhaust gas to the combustion device (30). It is supposed to be done. The amount of exhaust gas supplied to the combustion device (30) through the duct (26) is controlled by a fan (26a) interposed in the duct (26). The combustion device (30) burns the exhaust gas supplied via the duct (26) to incinerate harmful components such as solvent gas and tar components in the exhaust gas.

前記燃焼装置(30)には、そこから発生する高温燃焼
排ガスを排出するためのダクト(32)が引き出されて
おり、該ダクト(32)は、前記排気予熱用熱交換器(
31)を経由するように配管されている。そして、該ダ
クト(32)にて排出される高温燃焼排ガスは、前記排
気予熱用熱交換器(31)において、前記排気の加熱源
として使用されるようになっている。尚、該ダクト(3
2)による高温燃焼排ガスの排出量は、該ダクト(32
)に中途介装されているファン(32a)の制御によっ
て行われるようになっている。
A duct (32) for discharging high-temperature combustion exhaust gas generated therefrom is drawn out from the combustion device (30), and the duct (32) is connected to the exhaust preheating heat exchanger (
31). The high-temperature combustion exhaust gas discharged through the duct (32) is used as a heat source for the exhaust gas in the exhaust gas preheating heat exchanger (31). In addition, the duct (3
2) The amount of high temperature combustion exhaust gas discharged from the duct (32
) is controlled by a fan (32a) that is intermediately installed in the fan (32a).

前記ダクト(32)は、前記排気予熱用熱交換器(31
)の配置位置よりも更に下流側へ延びるように配管され
ている。そして、該ダクト(32)の配管は、その下流
域において、エア供給手段(40)の一部たるフレッシ
ュエア加熱用熱交換器(41)も経由するようになって
いる。
The duct (32) is connected to the exhaust preheating heat exchanger (31).
) The piping is arranged to extend further downstream than the location. The piping of the duct (32) also passes through a fresh air heating heat exchanger (41), which is part of the air supply means (40), in its downstream region.

前記ダクト(32)か中途経由するフレッシュエア加熱
用熱交換器(41)には、外気から取り入れられる外気
フレッシュエアの一部を案内するためのフレッシュエア
供給管(43)も中途経由するようになっている。該熱
交換器(41)においては、前記高温燃焼排ガスと前記
外気フレッシュエアとの間で熱交換が行われる。そして
、その熱交換によって加熱されてなる加熱フレッシュエ
アは、前記熱交換器(41)を経由せずに流量制御自在
なバイパスダンパ(42)を経由する前記外気フレッシ
ュエアと適量混合され、前記炉体(20)内の所定温度
維持に適した適宜温度となった混合フレッシュエアとさ
れる。そして、該混合フレッシュエアは、前記炉体(2
0)内の各ゾーンへの循環風路へ、更に詳しくは、前記
各ゾーン(21)。
A fresh air supply pipe (43) for guiding a part of fresh air taken in from the outside air is also connected to the fresh air heating heat exchanger (41) which passes through the duct (32) midway. It has become. In the heat exchanger (41), heat exchange is performed between the high temperature combustion exhaust gas and the fresh outside air. The heated fresh air heated by the heat exchange is mixed in an appropriate amount with the outside air fresh air that passes through the bypass damper (42) whose flow rate can be freely controlled without passing through the heat exchanger (41). The mixed fresh air has an appropriate temperature suitable for maintaining a predetermined temperature inside the body (20). Then, the mixed fresh air is supplied to the furnace body (2).
0), more specifically, each zone (21).

(23)、 (24)と通じる循環風路(21A)、 
(23A)、 (24A)へ分配導入される。そして、
前記炉体(20)内での対流熱風に補給されて炉内温度
がゾーン毎に所定温度に維持される。尚、前記フレッシ
ュエア供給管(43)によるフレッシュエアの供給量は
、該供給管(43)に中途介装されているファン(43
a)の制御によって行われるようになっている。
(23), (24) and a circulating air passage (21A),
(23A) and (24A). and,
The temperature inside the furnace is maintained at a predetermined temperature for each zone by being supplemented with convective hot air within the furnace body (20). Note that the amount of fresh air supplied by the fresh air supply pipe (43) is determined by the amount of fresh air supplied by the fresh air supply pipe (43).
This is done under the control of a).

さて、前記炉体(20)には、その炉入口(20a)及
び炉出口(20b)に、前記塗装物(A)の通過を検出
するセンサ(11)、 (12)が設けられており、該
センサ(11)、 (12)の検出信号は、前記炉体(
20)内における塗装物(A)の数量に応じて前記燃焼
装置(30)への排気空気の供給量及び前記エア供給手
段(40)によるフレッシュエアの前記対流熱風への補
給量を制御する制御手段の一例としての制御装置(10
)へ入力されるようになっている。
Now, the furnace body (20) is provided with sensors (11) and (12) at its furnace inlet (20a) and furnace outlet (20b) for detecting passage of the coated object (A), The detection signals of the sensors (11) and (12) are transmitted to the furnace body (
20) control for controlling the amount of exhaust air supplied to the combustion device (30) and the amount of fresh air supplied to the convective hot air by the air supply means (40) according to the number of coated objects (A) in the interior; A control device (10
).

前記制御装置(lO)は、入力される前記センサ(11
)、 (12)の検出信号を用いて炉体(20)内にお
ける塗装物(A)の数を算出し、その算出結果に基づい
て前記燃焼装置!(30)への排気空気の適正な供給量
及び前記エア供給手段(40)によるフレッシュエアの
前記対流熱風への適正な補給量をを求め、その結果に基
づき、前記排気空気用のダクト(26)に中途介装され
ているファン(26a)と、前記高温燃焼排ガス用のダ
クト(32)に中途介装されているファン(32a)と
、前記フレッシュエア供給管(43)に中途介装されて
いるファン(43a>との制御(即ち、炉体(20)内
における塗装物(A)の数が減少するほど、燃焼装置(
30)への排気空気の供給量及びエア供給手段(40)
によるフレッシュエアの補給量を互いに同調させて減少
させる制御)を行うようになっている。
The control device (1O) receives input from the sensor (11
), the number of coated objects (A) in the furnace body (20) is calculated using the detection signals of (12), and based on the calculation result, the combustion device! An appropriate amount of exhaust air to be supplied to the exhaust air duct (26) and an appropriate amount of fresh air to be supplied to the convection hot air by the air supply means (40) are determined, and based on the results, an appropriate amount of fresh air to be supplied to the exhaust air duct (26) is determined. ), a fan (32a) installed halfway in the high-temperature combustion exhaust gas duct (32), and a fan (32a) installed halfway in the fresh air supply pipe (43). (i.e., as the number of coated objects (A) in the furnace body (20) decreases, the combustion device (
Amount of exhaust air supplied to 30) and air supply means (40)
control to reduce the amount of fresh air supplied in synchronization with each other.

〔別実施例〕 前記制御装置(10)が、入力される前記センサ(11
)、 (12)の検出信号を用いて炉体(20)内にお
ける塗装物(A)の数を算出し、その数が零であるとき
に、前記燃焼装置(30)の燃焼温度を、前記焼却処理
に適した所定温度から、前記炉内温度維持に支障のない
程度まで下げると共に、前記塗装物(A)の炉内搬入か
予期された状態での前記燃焼装置(30)の燃焼温度を
前記所定温度に戻す温度設定手段(50)としての機能
を備えている実施例も考えられる。尚、前記燃焼装置t
(30)の燃焼温度を調整するのは、前記燃焼装置(3
0)か備えるバーナー(30a)の調整によって行われ
る。
[Another embodiment] The control device (10) receives input from the sensor (11).
), the number of coated objects (A) in the furnace body (20) is calculated using the detection signals of (12), and when the number is zero, the combustion temperature of the combustion device (30) is calculated as described above. Lowering the temperature from a predetermined temperature suitable for incineration to a level that does not interfere with maintaining the temperature inside the furnace, and also lowering the combustion temperature of the combustion device (30) when the painted object (A) is expected to be brought into the furnace. An embodiment may also be considered in which the temperature setting means (50) functions to return the temperature to the predetermined temperature. Incidentally, the combustion device t
The combustion temperature of the combustion device (30) is adjusted by adjusting the combustion temperature of the combustion device (30).
0) by adjusting the burner (30a) provided.

また、前記塗装物(A)の炉内搬入を予期するのに、例
えば、塗装物(A)の塗装乾燥炉への搬送装置に前記塗
装物(A)の通過を検知するセンサ(図外)を設けてお
き、該センサの検出結果によって前記炉内搬入を予期す
ることとしてもよく、また塗装物(A)の塗装スケジュ
ールを前記制御装置(10)に予めインプットしておき
、その情報に基づいて前記炉内搬入を予期することとし
てもよい。
In addition, in order to anticipate the conveyance of the painted object (A) into the furnace, for example, a sensor (not shown) that detects the passage of the painted object (A) is installed in the conveyance device for the painted object (A) to the coating drying furnace. may be provided, and the delivery into the furnace may be predicted based on the detection result of the sensor.Also, the coating schedule for the object to be coated (A) may be inputted into the control device (10) in advance, and the control device may be configured to control the process based on the information. It is also possible to anticipate the delivery into the furnace.

又、前記炉体(20)内の塗装物(A)の数量を検出す
る手段としては、前記炉体(20)の炉入口(20a)
及び炉出口(20b)に設;すた、前記塗装物(A)の
通過検出用のセンサ(II)、 (12) ヲ用いる手
段以外の手段も考えられる。例えば、前記炉体(20)
の炉入口(20a )に設げたセンサ(II)の検出結
果と、前記塗装物(A)の炉内搬送速度とから、前記炉
体(20)内の塗装*(A)の数量を求めたり、又、予
め設定された乾燥処理スケジュールに基ついて各時点に
おける炉体(2o)内の塗装物(A)数量を判定すると
いう手段も考えられる。
Further, as a means for detecting the quantity of coated objects (A) in the furnace body (20), the furnace inlet (20a) of the furnace body (20) is used.
and a sensor (II) for detecting passage of the coated object (A) installed at the furnace outlet (20b). For example, the furnace body (20)
From the detection result of the sensor (II) installed at the furnace inlet (20a) and the conveyance speed of the coated object (A) in the furnace, the quantity of coating*(A) in the furnace body (20) is determined. Alternatively, a method may be considered in which the quantity of coated objects (A) in the furnace body (2o) at each point in time is determined based on a preset drying treatment schedule.

尚、特許請求の範囲の項に図面との対照を便利にする為
に符号を記すか、該記入により本発明は添付図面の構造
に限定されるものではない。
It should be noted that the present invention is not limited to the structure shown in the accompanying drawings by adding reference numerals in the claims for convenient comparison with the drawings.

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

第1図は本発明に係る塗装乾燥炉の一実施例を示す全体
構成図、第2図は従来の塗装乾燥炉を示す全体構成図で
ある。 (10)・・・・・・制御手段、(2o)・・・・・・
炉体、(3o)・・団・燃焼装置、(4o)・・・・・
・エア供給手段、(5o)・旧・・温度設定手段、(A
)・・・・・・塗装物。
FIG. 1 is an overall configuration diagram showing an embodiment of a paint drying oven according to the present invention, and FIG. 2 is an overall configuration diagram showing a conventional paint drying oven. (10)... Control means, (2o)...
Furnace body, (3o)... group/combustion device, (4o)...
・Air supply means, (5o) ・Old temperature setting means, (A
)...Painted object.

Claims (1)

【特許請求の範囲】 1、炉体(20)内の塗装物(A)を対流熱風によって
加熱乾燥するときに発生する溶剤ガスを含む排気空気が
供給され、該排気空気を燃焼させて焼却処理した上で高
温燃焼排ガスとして排出する燃焼装置(30)を備え、 前記燃焼装置(30)からの高温燃焼排ガスと熱交換さ
せて加熱したフレッシュエアを炉内温度維持のために前
記対流熱風へ補給するエア供給手段(40)を備えた塗
装乾燥炉であって、前記炉内における塗装物(A)の数
量に応じて、前記燃焼装置(30)への排気空気の供給
量及び前記エア供給手段(40)によるフレッシュエア
の前記対流熱風への補給量を制御する制御手段(10)
を備える塗装乾燥炉。 2、前記塗装物(A)が前記炉体(20)内に存在しな
い状態での前記燃焼装置(30)の燃焼温度を、前記焼
却処理に適した所定温度から、前記炉内温度維持に支障
のない程度まで下げると共に、前記塗装物(A)の炉内
搬入が予期された状態での前記燃焼装置(30)の燃焼
温度を前記所定温度に戻す温度設定手段(50)を備え
ている請求項1記載の塗装乾燥炉。
[Claims] 1. Exhaust air containing solvent gas generated when the coated article (A) in the furnace body (20) is heated and dried by convection hot air is supplied, and the exhaust air is combusted and incinerated. A combustion device (30) is provided to discharge the heated combustion exhaust gas as high-temperature combustion exhaust gas, and fresh air heated by exchanging heat with the high-temperature combustion exhaust gas from the combustion device (30) is supplied to the convection hot air in order to maintain the temperature inside the furnace. A paint drying furnace equipped with an air supply means (40) for controlling the amount of exhaust air supplied to the combustion device (30) and the air supply means according to the number of coated objects (A) in the furnace. Control means (10) for controlling the amount of fresh air supplied to the convection hot air according to (40)
A paint drying oven equipped with 2. The combustion temperature of the combustion device (30) in a state where the painted material (A) is not present in the furnace body (20) is changed from a predetermined temperature suitable for the incineration process to a temperature that interferes with maintaining the temperature inside the furnace. The method further comprises a temperature setting means (50) which lowers the combustion temperature of the combustion device (30) to the predetermined temperature in a state in which the painted object (A) is expected to be carried into the furnace. The paint drying oven according to item 1.
JP2169643A 1990-06-27 1990-06-27 Paint drying oven Expired - Fee Related JP3043372B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2169643A JP3043372B2 (en) 1990-06-27 1990-06-27 Paint drying oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2169643A JP3043372B2 (en) 1990-06-27 1990-06-27 Paint drying oven

Publications (2)

Publication Number Publication Date
JPH0461953A true JPH0461953A (en) 1992-02-27
JP3043372B2 JP3043372B2 (en) 2000-05-22

Family

ID=15890287

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2169643A Expired - Fee Related JP3043372B2 (en) 1990-06-27 1990-06-27 Paint drying oven

Country Status (1)

Country Link
JP (1) JP3043372B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101856309B1 (en) * 2016-03-09 2018-06-25 김경현 Transformable and extendable modular furniture

Also Published As

Publication number Publication date
JP3043372B2 (en) 2000-05-22

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