JPS6127673B2 - - Google Patents
Info
- Publication number
- JPS6127673B2 JPS6127673B2 JP2779082A JP2779082A JPS6127673B2 JP S6127673 B2 JPS6127673 B2 JP S6127673B2 JP 2779082 A JP2779082 A JP 2779082A JP 2779082 A JP2779082 A JP 2779082A JP S6127673 B2 JPS6127673 B2 JP S6127673B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace body
- exhaust gas
- furnace
- exhaust
- temperature
- 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
Landscapes
- Drying Of Solid Materials (AREA)
Description
【発明の詳細な説明】
この発明は、炉体内に加熱気体を供給しながら
排気を行ない炉体内温度を設定値に保つと共に、
炉体内からの排ガスを排ガス処理装置で処理する
ようにした焼付乾燥炉に関する。DETAILED DESCRIPTION OF THE INVENTION This invention maintains the temperature inside the furnace at a set value by exhausting the furnace while supplying heated gas, and
The present invention relates to a baking drying furnace in which exhaust gas from the furnace body is treated by an exhaust gas treatment device.
この種焼付乾燥炉は、電着等によつて被塗装物
に付着させた塗料を焼付乾燥させる場合に使用す
るもので、その際発生する蒸発した樹脂分や可塑
剤等の有害物質を含んだ排ガスは排ガス処理装置
に導かれて処理された後大気中に放出される。 This type of baking drying oven is used to bake and dry paint that has been applied to objects by electrodeposition, etc., and contains harmful substances such as evaporated resin and plasticizers that are generated during this process. The exhaust gas is led to an exhaust gas treatment device, treated, and then released into the atmosphere.
従来の自動車車体等の塗装ラインで使用される
大型の焼付乾燥炉は、第1図に示す如く、被塗装
物がコンベア等の搬送体(図示せず)によつて搬
入出される炉体1の出入口に夫々エアカーテンを
形成するフアン2,3が配設されていると共に、
炉体1内が複数の領域A1〜A4に分割され、各領
域Ai(i=1、2、3、4)には夫々加熱気体
供給装置4及び排気ダクト5が配設された構成を
有する。 As shown in FIG. 1, a large-scale baking drying oven used in a conventional painting line for automobile bodies, etc. has a furnace body 1 in which objects to be coated are carried in and out by a conveyor (not shown). Fans 2 and 3 forming air curtains are disposed at the entrance and exit, respectively, and
The inside of the furnace body 1 is divided into a plurality of areas A1 to A4 , and each area Ai (i=1, 2, 3, 4) is provided with a heated gas supply device 4 and an exhaust duct 5, respectively. have
又炉体1の出入口のフード6,7にも排気ダク
ト8が夫々配設され、各排気ダクト5,8が1本
の排ガスダクト9に連接されその端部に配設され
たフアン10によつて炉体1内の有害物質含有ガ
ス等の排ガスが吸引排気される。 In addition, exhaust ducts 8 are also provided in the hoods 6 and 7 at the entrance and exit of the furnace body 1, and each exhaust duct 5 and 8 is connected to one exhaust gas duct 9 and is connected to a fan 10 installed at the end of the exhaust duct 9. Exhaust gas such as gas containing harmful substances in the furnace body 1 is then sucked and exhausted.
吸引された排ガスは熱交換器11介して一旦昇
温され、次いでブロワー12によつて空気が給さ
れた燃焼装置13によつて再加熱され、さらに触
媒14によつて有害成分を分解除去した後、前記
熱交換器11を通つて大気に放射される。なお、
フアン10、熱交換器11、燃焼装置13、触媒
14等を含んで排ガス処理装置15が構成されて
いる。 The sucked exhaust gas is once heated through a heat exchanger 11, then reheated by a combustion device 13 supplied with air by a blower 12, and after decomposition and removal of harmful components by a catalyst 14. , is radiated to the atmosphere through the heat exchanger 11. In addition,
An exhaust gas treatment device 15 includes a fan 10, a heat exchanger 11, a combustion device 13, a catalyst 14, and the like.
以上の従来装置によると、炉体1の出入口から
外部に漏洩する有害気体を排気ダクト8で補集す
るようにしているので、乾燥炉近傍の環境衛生の
保全に効果があるものであるが、排気ダクト8か
ら補集される排ガスは、外気を含んでいるため温
度が低く例えば炉体1内温度を170℃に維持して
いるものとすれば、排気ダクト8からの排ガス温
度は70℃〜80℃となり、しかも炉体1内の各領域
Aiにおける排気量は加熱気体供給装置4によつ
て炉体1内に供給される空気量と略々等しく例え
ば12.5m3/minであるが、出入口排ガス排気量は
有害物質含有ガスの外部への漏洩を防止するため
には例えば50m3/minが必要となり、従つて排気
ダクト8からの排ガスは低温、大排気量となる。
このため排ガスダクト9には前記蒸発した樹脂分
や可塑剤等と高沸点の揮発性水性物とが凝縮して
ヤニとなつて内壁に付着し、ダクト内壁へのヤニ
の付着や熱交換器や触媒層へのヤニの付着によつ
て火災の発生原因となつたり、熱交換器や触媒層
の作動不良を起したりするので定期的な清掃を行
なう必要がありこれが面倒である欠点を有するも
のであつた。 According to the conventional apparatus described above, the exhaust duct 8 collects harmful gases leaking to the outside from the entrance and exit port of the furnace body 1, which is effective in preserving the environmental hygiene in the vicinity of the drying furnace. The temperature of the exhaust gas collected from the exhaust duct 8 is low because it contains outside air. For example, if the temperature inside the furnace body 1 is maintained at 170℃, the temperature of the exhaust gas from the exhaust duct 8 is 70℃~ 80℃, and each area in the furnace body 1
The exhaust volume at Ai is approximately equal to the air volume supplied into the furnace body 1 by the heated gas supply device 4, for example, 12.5 m 3 /min, but the exhaust gas volume at the entrance and exit is approximately equal to the air volume supplied into the furnace body 1 by the heating gas supply device 4, but the exhaust gas volume at the entrance and exit is the same as the amount of air supplied into the furnace body 1 by the heating gas supply device 4. In order to prevent leakage, for example, 50 m 3 /min is required, so the exhaust gas from the exhaust duct 8 has a low temperature and a large exhaust volume.
Therefore, in the exhaust gas duct 9, the evaporated resin, plasticizer, etc. and high boiling point volatile aqueous substances condense and become tar and adhere to the inner wall of the duct. The disadvantage is that periodic cleaning is required, which is troublesome, as resin adhesion to the catalyst layer can cause a fire or malfunction of the heat exchanger or catalyst layer. It was hot.
本発明は前記従来装置の欠点を解消せんとする
もので、その特徴とする所は乾燥炉出入口におけ
る低温排ガスを炉体内へ加熱気体を供給する加熱
気体供給装置に供給して炉体へ環流させるように
したことである。 The present invention aims to eliminate the drawbacks of the conventional apparatus, and is characterized by supplying the low-temperature exhaust gas at the entrance and exit of the drying furnace to a heated gas supply device that supplies heated gas into the furnace body, and circulating it back to the furnace body. This is what I did.
以下図面について本発明の実施例を説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第2図は本発明による焼付乾燥炉を示す系統図
であつて、第1図との対応部分には同一符号を付
しその詳細説明は省略するが、炉1出入口の排気
ダクト8が省略されている。又各領域Aiの加熱
気体供給装置4が炉体内気体及びブロワー16か
らの新鮮空気が供給される燃焼装置17と、この
燃焼装置17から得られる加熱気体を炉体1内に
送風するフアン18とから構成されている。な
お、フアン18と炉体1との間にはパージ用ダン
パー19が介挿され余剰加熱気体を排ガスダスト
9に逃がすようにされている。 FIG. 2 is a system diagram showing a baking drying furnace according to the present invention, in which parts corresponding to those in FIG. ing. The heated gas supply device 4 in each area Ai also includes a combustion device 17 to which the gas inside the furnace and fresh air from the blower 16 are supplied, and a fan 18 that blows the heated gas obtained from the combustion device 17 into the furnace body 1. It consists of A purge damper 19 is interposed between the fan 18 and the furnace body 1 to release excess heated gas to the exhaust gas dust 9.
又炉体1の出入口のフード6,7内の排ガス
は、排ガスダクト20,21を通じて例えば炉体
1と領域A1及びA4の燃焼装置17の吸気側との
間を接続する給気通路22に供給され、この燃焼
装置17で再加熱されて炉体1内に環流される。 Further, the exhaust gas in the hoods 6 and 7 at the entrance and exit of the furnace body 1 is transferred through exhaust gas ducts 20 and 21 to an air supply passage 22 that connects the furnace body 1 and the intake side of the combustion device 17 in areas A 1 and A 4 , for example. The fuel is supplied to the furnace body 1, is reheated by the combustion device 17, and then circulated into the furnace body 1.
この場合炉体1の領域A及びAへの加熱気体供
給量がフード6及び7からの排ガス量分増加すの
で、これら領域A1及びA4に配設された排気ダク
ト5の排気量が他の領域A2及びA3のそれに比し
多くなるように選定されている。 In this case, the amount of heated gas supplied to areas A and A of the furnace body 1 increases by the amount of exhaust gas from the hoods 6 and 7, so the exhaust volume of the exhaust duct 5 disposed in these areas A 1 and A 4 is The area is selected so that it is larger than that in areas A 2 and A 3 .
次に以上の本発明構成による作用を説明する
と、炉体出入口の外気を含んだ低温排ガスがその
近傍即ち領域A及びAの加熱気体供給装置4の燃
焼装置17を通し再加熱されて炉体1内に環流さ
れ、炉体1内の高温排ガスのみが排ガスダクト9
を通じて処理装置15に供給されるので、排ガス
ダクト9内の排ガス温度の低下を防止することが
できる。 Next, to explain the effect of the above configuration of the present invention, the low-temperature exhaust gas containing outside air at the entrance and exit of the furnace body is reheated through the combustion device 17 of the heated gas supply device 4 in the vicinity of the area A and A, and the furnace body 1 is reheated. Only the high-temperature exhaust gas inside the furnace body 1 is circulated into the exhaust gas duct 9.
Since the exhaust gas is supplied to the processing device 15 through the exhaust gas duct 9, the exhaust gas temperature in the exhaust gas duct 9 can be prevented from decreasing.
以上のように本発明によると、炉体出入口にお
ける低温排ガスは、炉体内へ加熱気体を供給する
加熱気体供給装置に供給され、該加熱気体供給装
置で再加熱されて炉体内へ環流されるもので、炉
体内の温度を設定値に容易に維持させることがで
きると共に、炉体内の高温排ガスのみを排ガスダ
クトを通じて排ガス処理装置に送風することがで
きるのでニヤの発生を減少させることができ排ガ
スダクト、排ガス処理装置等へのヤニの付着を従
来装置に比較して格段に少なくし得、従つて火災
の危険性を回避し得ると共に排ガス処理装置の作
動不良を防止することができ、清掃回数を大幅に
減少でき乾燥炉の稼動率を向上せしめ得る等の優
れた特徴を有する。 As described above, according to the present invention, the low-temperature exhaust gas at the inlet and outlet of the furnace body is supplied to the heated gas supply device that supplies heated gas into the furnace body, and is reheated by the heated gas supply device and circulated back into the furnace body. The temperature inside the furnace can be easily maintained at the set value, and only the high-temperature exhaust gas inside the furnace can be blown to the exhaust gas treatment equipment through the exhaust gas duct, which reduces the occurrence of dust. , it is possible to significantly reduce the amount of tar adhering to the exhaust gas treatment equipment, etc. compared to conventional equipment, thereby avoiding the risk of fire, preventing malfunction of the exhaust gas treatment equipment, and reducing the number of times of cleaning. It has excellent features such as being able to significantly reduce the amount of water and improving the operating rate of the drying oven.
尚上例においては、フード6,7から補集する
外気を含んだ排ガスを燃焼装置17の吸込側に供
給するようにした場合について説明したが、燃焼
装置17の出口側に供給し、これによる温度低下
を予め燃焼装置からの加熱気体温度を高く設定す
ることによつて防ぐようにしても良い。 In the above example, a case was explained in which exhaust gas containing outside air collected from the hoods 6 and 7 was supplied to the suction side of the combustion device 17. The temperature drop may be prevented by setting the temperature of the heated gas from the combustion device high in advance.
又炉体1内の領域数は4つに限らず炉体1の長
さに応じて適宜選択し得る。 Further, the number of regions in the furnace body 1 is not limited to four, but can be selected as appropriate depending on the length of the furnace body 1.
第1図は従来の焼付乾燥炉を示す系統図、第2
図は本発明による焼付乾燥炉を示す系統図であ
る。
1……炉体、4……加熱気体供給装置、5,8
……排気ダクト、9……排ガスダクト、15……
排ガス処理装置、17……燃焼装置、20,21
……排ガスダクト。
Figure 1 is a system diagram showing a conventional baking drying furnace;
The figure is a system diagram showing a baking drying oven according to the present invention. 1...Furnace body, 4...Heating gas supply device, 5, 8
...Exhaust duct, 9...Exhaust gas duct, 15...
Exhaust gas treatment device, 17... Combustion device, 20, 21
...Exhaust gas duct.
Claims (1)
い炉体内温度を設定値に保つと共に、炉体内から
の排ガスを排ガス処理装置で処理するようにした
焼付乾燥炉において、前記炉体の出入口における
低温排ガスを該炉体内へ加熱気体を供給する加熱
気体供給装置に供給して炉体内へ環流させるよう
にしたことを特徴とする焼付乾燥炉。1. In a baking drying furnace that maintains the temperature of the furnace body at a set value by exhausting the furnace body while supplying heated gas, and at the same time treating the exhaust gas from the furnace body with an exhaust gas treatment device, the temperature at the entrance and exit of the furnace body is low. A baking drying furnace characterized in that the exhaust gas is supplied to a heated gas supply device that supplies heated gas into the furnace body, and is circulated into the furnace body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2779082A JPS58145878A (en) | 1982-02-23 | 1982-02-23 | Baking drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2779082A JPS58145878A (en) | 1982-02-23 | 1982-02-23 | Baking drier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58145878A JPS58145878A (en) | 1983-08-31 |
| JPS6127673B2 true JPS6127673B2 (en) | 1986-06-26 |
Family
ID=12230763
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2779082A Granted JPS58145878A (en) | 1982-02-23 | 1982-02-23 | Baking drier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58145878A (en) |
-
1982
- 1982-02-23 JP JP2779082A patent/JPS58145878A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58145878A (en) | 1983-08-31 |
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