JPH0457386B2 - - Google Patents

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Publication number
JPH0457386B2
JPH0457386B2 JP59190977A JP19097784A JPH0457386B2 JP H0457386 B2 JPH0457386 B2 JP H0457386B2 JP 59190977 A JP59190977 A JP 59190977A JP 19097784 A JP19097784 A JP 19097784A JP H0457386 B2 JPH0457386 B2 JP H0457386B2
Authority
JP
Japan
Prior art keywords
heating
chamber
air
zone
heating zone
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 - Lifetime
Application number
JP59190977A
Other languages
Japanese (ja)
Other versions
JPS6170375A (en
Inventor
Noboru Maki
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.)
Rozai Kogyo Kaisha Ltd
Original Assignee
Rozai Kogyo Kaisha Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Rozai Kogyo Kaisha Ltd filed Critical Rozai Kogyo Kaisha Ltd
Priority to JP19097784A priority Critical patent/JPS6170375A/en
Publication of JPS6170375A publication Critical patent/JPS6170375A/en
Publication of JPH0457386B2 publication Critical patent/JPH0457386B2/ja
Granted legal-status Critical Current

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  • Coating Apparatus (AREA)
  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は連続乾燥オーブン、詳しくは塗装され
た材料からの蒸発ヒユームの壁面への付着を防止
した連続乾燥オーブンに関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a continuous drying oven, and more particularly to a continuous drying oven that prevents evaporated fume from adhering to walls from painted materials.

(従来の技術) 塗装された材料を連続乾燥するためのオーブン
は、第4図および第5図に示しているように、加
熱帯A、空冷帯Bが連設されてなり、塗装装置
(図示せず)において表面塗装された例えば板材
1を搬送コンベヤー2によりオーブンに向つて移
送し、加熱帯Aと空冷帯Bを通過可能に設けられ
た無端状の回動コンベヤー3に受け渡し、回動コ
ンベヤー3の移動中に加熱乾燥したのち冷却して
送り出すようになつている。上記した回動コンベ
ヤー3には定間隔をおいて塗装板材1を立姿状態
で支持するための支持捍4が設けられ、搬送コン
ベヤー2上の板材1は受け渡し室5において順次
個々該回動コンベヤー3の支持捍4に移載された
のち起立状態とされ、回動コンベヤー3の移動に
よつて加熱帯Aおよび空冷帯Bを通過する。加熱
帯Aには、熱風送風機6、下部蓄圧室7、板材加
熱室8および排気室9を備え、送風機6から送り
出された熱風は第4図に示しているようにまず下
部蓄圧室7に送られ、次いで板材加熱室8を通つ
たのち排気室9に至り、該送風機6によつて再び
下部蓄圧室7に送入され循環される。加熱室8を
通過中の板材1は上記循環熱風により加熱昇温さ
れるが、その際塗料から可燃性ヒユームが蒸発す
るため、その燃焼爆発を防止するべく循環熱風内
の可燃性ヒユームの対空気を爆発限界下限以下に
常時維持する必要があり、そのため濃度希釈用の
空気が混入されている。そして循環熱風の容量を
一定に保つために、加熱帯A内で最も蒸発ヒユー
ム量の多い個所、具体的には加熱室Aの入口の板
材1の受け渡し室5および板材1の加熱室Aへの
入口付近の雰囲気を排風機10によつて外部に排
出し、図示せざる脱臭装置に移送して脱臭処理さ
れるようになつている。
(Prior art) As shown in FIGS. 4 and 5, an oven for continuous drying of coated materials consists of a heating zone A and an air cooling zone B, which are connected to each other in a coating device ( For example, a plate material 1 whose surface has been painted is transferred to an oven by a conveyor 2, and delivered to an endless rotary conveyor 3 provided so as to be able to pass through a heating zone A and an air cooling zone B. After being heated and dried during transportation in step 3, it is cooled and sent out. The rotary conveyor 3 described above is provided with support racks 4 at regular intervals for supporting the coated plate materials 1 in an upright state, and the plate materials 1 on the transport conveyor 2 are transferred to the rotary conveyor 3 one after another in the delivery chamber 5. After being transferred to the support rack 4, it is placed in an upright state, and as the rotary conveyor 3 moves, it passes through the heating zone A and the air cooling zone B. The heating zone A is equipped with a hot air blower 6, a lower pressure accumulation chamber 7, a plate heating chamber 8, and an exhaust chamber 9, and the hot air sent out from the blower 6 is first sent to the lower pressure accumulation chamber 7 as shown in FIG. Then, after passing through the plate heating chamber 8, it reaches the exhaust chamber 9, and is again sent to the lower pressure accumulation chamber 7 by the blower 6 and circulated. The plate material 1 passing through the heating chamber 8 is heated and heated by the circulating hot air, but at this time flammable fume from the paint evaporates, so in order to prevent combustion explosion, the flammable fume in the circulating hot air is heated against the air. must be maintained below the lower explosive limit at all times, so air is mixed in to dilute the concentration. In order to keep the volume of circulating hot air constant, the area where the amount of evaporated fume is the largest in the heating zone A, specifically, the transfer chamber 5 of the plate material 1 at the entrance of the heating chamber A, and the transfer chamber 5 of the plate material 1 to the heating chamber A at the entrance of the heating chamber A. The atmosphere near the entrance is exhausted to the outside by an exhaust fan 10 and transferred to a deodorizing device (not shown) for deodorizing treatment.

したがつて受け渡し室5の入口11から外気が
流入すると同時に該受け渡し室5と加熱室8との
境界開口部12から該受け渡し室5内に多量の熱
風が流入し、その際該開口部12が大きいため、
該受け渡し室5内の低温雰囲気が該加熱室8内に
流れ込むという現象が生じている。
Therefore, at the same time as outside air flows in from the entrance 11 of the delivery chamber 5, a large amount of hot air flows into the delivery chamber 5 from the boundary opening 12 between the delivery chamber 5 and the heating chamber 8. Because it is large,
A phenomenon occurs in which the low-temperature atmosphere in the delivery chamber 5 flows into the heating chamber 8.

(発明が解決すべき問題点) 上記した受け渡し室5から加熱室8内に低温雰
囲気の流れ込み現象は、加熱室8内の温度低下を
招き、その温度低下によつて受け渡し室5の内壁
表面および加熱室8の炉内壁表面に可燃性ヒユー
ムが付着するという不都合が生じる。そしてこれ
らの壁面に可燃性ヒユームが付着すると、この付
着ヒユームからも可燃性ガスの蒸発が生じ、加熱
室8内は塗装板材1から蒸発する可燃性ヒユーム
と上記付着ヒユームから蒸発する不定量な可燃性
ヒユームとが混合されて部分的に可燃性ヒユーム
が高濃度となり、この高濃度な可燃性ヒユームの
存在を予測して爆発限界下限を維持するための空
気、即ち、板材1から発生する可燃性ヒユームの
爆発限界下限値よりも数倍の対空気比に相当する
多量の稀釈空気を導入して安全性を確保している
の実情である。
(Problems to be Solved by the Invention) The phenomenon of the low-temperature atmosphere flowing into the heating chamber 8 from the delivery chamber 5 described above causes a temperature drop in the heating chamber 8, and the temperature drop causes the inner wall surface of the delivery chamber 5 to This causes the inconvenience that flammable fume adheres to the inner wall surface of the heating chamber 8. When flammable fume adheres to these walls, flammable gas evaporates from this adhered fume, and the inside of the heating chamber 8 contains flammable fume evaporated from the painted board material 1 and an indefinite amount of combustible gas evaporated from the adhered fume. In order to predict the presence of this high concentration of combustible fume and maintain the lower explosive limit, the combustible fume generated from the plate material 1 is The reality is that safety is ensured by introducing a large amount of diluted air, which is equivalent to an air-to-air ratio several times higher than the lower explosive limit of Huyum.

また加熱帯Aと空冷帯Bとの接続部13は、板
材1が立姿状態での通過を許容しなければならぬ
ことから、その接続部13の開口部14は実質的
に該加熱室8の縦断面積と同等の大きさとなり、
そのため必然的に加熱帯Aと空冷帯Bとの間に内
部雰囲気の流動が生じ、それによつて加熱帯Aで
は温度低下、空冷帯Bでは温度上昇が生じること
になり、オーブン内の加熱および冷却の有効作用
域の長さが短かくなるという問題点を有し、上記
した有効作用域の長さを充分なものとするために
は、オーブン炉全体の長さを大きくしなければな
らないことになり、更に多量の熱風および稀釈空
気が必要となるばかりではなくバーナーの焚量が
増大して不経済となり、その上、定期的に壁面に
付着したヒユームの除去作業のために多くの時間
と労力を要する。
Furthermore, since the connecting portion 13 between the heating zone A and the air cooling zone B must allow the passage of the plate material 1 in an upright state, the opening 14 of the connecting portion 13 is substantially the same as that of the heating chamber 8. The size is equivalent to the vertical cross-sectional area,
Therefore, a flow of internal atmosphere inevitably occurs between heating zone A and air-cooling zone B, which causes a temperature drop in heating zone A and a temperature increase in air-cooling zone B, resulting in heating and cooling inside the oven. There is a problem that the length of the effective working area becomes short, and in order to make the length of the effective working area sufficient as described above, the length of the entire oven furnace must be increased. This not only requires a larger amount of hot air and diluted air, but also increases the amount of burner combustion, making it uneconomical.In addition, it takes a lot of time and effort to periodically remove the fume that adheres to the wall. It takes.

(問題点を解決するための手段) 本発明の目的は、上記したオーブンの壁面への
ヒユーム付着を効果的に防止すると共に、加熱帯
と空冷帯との間の雰囲気流通を防止して従来のオ
ーブンにおける上記した種々な問題点を改善する
ことにあり、次のように構成してなるものであ
る。即ち、第1図および第2図に示しているよう
に、乾燥オーブン加熱帯Aの受け渡し室5の内壁
15と該受け渡し室5と加熱室8との境界開口部
12の近傍の加熱室8の内壁16および排気ダク
ト17の内周壁18をそれぞれ空気流通可能な空
間19,19を介在せしめた2重構造となし、該
空間19,19内に脱臭装置から出る高温排ガス
を導入して、上記各内壁15,16,18の表面
温度を180℃以上に接続せしめるようになし、更
に加熱帯Aと空冷帯Bとを実質的に分離して該加
熱帯Aおよび空冷帯Bのそれぞれに一対の支持捍
4a,4bを備えた加熱帯側コンベヤー3Aおよ
び受止捍4を備えた冷却帯コンベヤー3Bを設け
るとともに、両コンベヤー3A,3B間に板材1
を水平状態となして移送する中間搬送コンベヤー
20を設けて加熱帯Aと空冷帯Bとの接続開口部
21,26の開口面積を縮小し、該加熱帯Aの出
入口に上下一対の蓄圧室22,22を対向設置し
て加熱帯Aと空冷帯Bとの接続部における空気の
自由流通を防止するよう構成してなるものであ
る。
(Means for Solving the Problems) An object of the present invention is to effectively prevent fume from adhering to the wall surface of the oven as described above, and to prevent the atmosphere from flowing between the heating zone and the air cooling zone. The object of this invention is to improve the various problems mentioned above in ovens, and is constructed as follows. That is, as shown in FIGS. 1 and 2, the inner wall 15 of the transfer chamber 5 of the drying oven heating zone A and the heating chamber 8 near the boundary opening 12 between the transfer chamber 5 and the heating chamber 8. The inner wall 16 and the inner circumferential wall 18 of the exhaust duct 17 have a double structure with spaces 19 and 19 through which air can flow, respectively, and the high temperature exhaust gas from the deodorizing device is introduced into the spaces 19 and 19. The surface temperature of the inner walls 15, 16, and 18 is connected to 180° C. or higher, and further, the heating zone A and the air cooling zone B are substantially separated, and a pair of supports are provided for each of the heating zone A and the air cooling zone B. A heating zone conveyor 3A equipped with grooves 4a and 4b and a cooling zone conveyor 3B equipped with a receiving groove 4 are provided, and a plate material 1 is provided between both conveyors 3A and 3B.
An intermediate conveyor 20 is provided to transport the water in a horizontal state to reduce the opening area of the connecting openings 21 and 26 between the heating zone A and the air cooling zone B. , 22 are arranged facing each other to prevent free flow of air at the connection between the heating zone A and the air cooling zone B.

(作用) 続いて、上記のごとく構成してなる本発明の乾
燥オーブンについて、その作用を述べながら更に
具体的に説明すると、乾燥オーブンの加熱帯Aに
おける受け渡し室5の内壁15の全域、該受け渡
し室5の上方に設けられた排気ダクト17の内周
壁18および受け渡し室5と加熱室8との境界部
の開口部12近傍の加熱室8の内壁16の表面側
にそれぞれ空間19,19,19を保つて耐蝕性
金属板を張設して二重構造となし、更に板材1の
入口開口部11の上下に蓄圧室23,23を設け
て上記各空間19,19,19と該蓄圧室23,
23とを連通せしめ、脱臭装置から排出される高
温ガスを該空間19,19,19に導き入れて該
蓄圧室23,23から放出させ、それによつて上
記各内壁15,16および内周壁18の表面温度
を180℃以上に持続させるとともに蓄圧室23,
23のノズルから噴出する10米/分程度の熱風に
よつて受け渡し室5の入口開口部11における内
外空気の流通を遮断する。かくして加熱室8内の
温度低下が防止され、塗装板材1から蒸発した可
燃性ヒユームは壁面に接触しても凝固付着するこ
とがなく、排風機10による排気作用によつて高
温雰囲気と共に脱臭装置に向つて排出される。
(Function) Next, the drying oven of the present invention configured as described above will be explained in more detail while describing its function. Spaces 19, 19, 19 are provided on the inner peripheral wall 18 of the exhaust duct 17 provided above the chamber 5 and on the surface side of the inner wall 16 of the heating chamber 8 near the opening 12 at the boundary between the delivery chamber 5 and the heating chamber 8, respectively. A corrosion-resistant metal plate is stretched to create a double structure, and pressure accumulators 23, 23 are provided above and below the inlet opening 11 of the plate 1, and the above-mentioned spaces 19, 19, 19 and the pressure accumulator 23 are provided. ,
23, the high-temperature gas discharged from the deodorizing device is introduced into the spaces 19, 19, 19 and released from the pressure accumulation chambers 23, 23, thereby causing the inner walls 15, 16 and the inner circumferential wall 18 to be in communication with each other. While maintaining the surface temperature at 180℃ or higher, the pressure accumulation chamber 23,
The flow of internal and external air at the entrance opening 11 of the delivery chamber 5 is blocked by the hot air jetted from the nozzle 23 at a rate of about 10 m/min. In this way, the temperature inside the heating chamber 8 is prevented from decreasing, and the combustible fume evaporated from the painted board material 1 does not solidify and adhere even if it comes into contact with the wall surface, and due to the exhaust action of the exhaust fan 10, it is sent to the deodorizing device along with the high temperature atmosphere. It is ejected towards.

また加熱帯Aの上記した2重構造の内壁15,
16以外の個所の壁温は、第2図に示しているよ
うに、循環送風機6に両側蓄圧室24,24から
下方に高温雰囲気を噴出せしめ、該高温雰囲気を
板材加熱室8の床面から上方に噴出せしめて板材
1,1を加熱し、排気室25に流動せしめ、送風
機6側に帰流する雰囲気流と、排風機10から脱
臭装置に移動する気流とに分れるが、オーブン内
壁表面は常に高温雰囲気の接触下にあるため180
℃以上の温度を保持し、ヒユーム付着は発生しな
い。
In addition, the above-mentioned double-structured inner wall 15 of the heating zone A,
As shown in FIG. 2, the wall temperature at locations other than 16 can be reduced by causing the circulation blower 6 to blow out a high temperature atmosphere downward from the pressure accumulation chambers 24, 24 on both sides, and then blowing the high temperature atmosphere from the floor of the board heating chamber 8. The atmosphere is ejected upward to heat the plates 1, 1, flows into the exhaust chamber 25, and is divided into an atmosphere flow that returns to the blower 6 side and an air flow that moves from the exhaust fan 10 to the deodorizing device. 180 because it is always in contact with a high temperature atmosphere.
Maintains temperature above ℃ and no fume build-up occurs.

他方オーブンの加熱帯Aと空冷帯Bとを図示し
たごとく実質的に分離し、それぞれに前記したご
とき支持捍4a,4bを備えた加熱帯側コンベヤ
ー3Aおよび受止捍4を備えた冷却帯側コンベヤ
ー3Bを同一方向に同調回動するように設備する
とともに両コンベヤー3A,3B間に板材1を水
平状態にて順次移送可能な中間搬送コンベヤー2
0を設け、加熱帯側コンベヤー3Aの末端部にお
いて該中間コンベヤー20上に水平状態で移行さ
せて板材1を空冷室Bに搬送し、空冷帯側コンベ
ヤー3Bに移行したのち、該コンベヤー3Bの受
止捍4の起立作用によつて再び起立状態となして
空冷室B内を通過させるように構成する。
On the other hand, the heating zone A and the air-cooling zone B of the oven are substantially separated as shown, and the heating zone side conveyor 3A is provided with the above-mentioned support plates 4a and 4b, and the cooling zone side is provided with the catch plate 4, respectively. An intermediate transport conveyor 2 is installed so that the conveyors 3B rotate in synchronization in the same direction, and can sequentially transport the plate material 1 in a horizontal state between both conveyors 3A and 3B.
0 is provided at the end of the heating zone side conveyor 3A, and the plate material 1 is transferred horizontally onto the intermediate conveyor 20 at the end of the heating zone side conveyor 3A to convey the plate material 1 to the air cooling chamber B, and then transferred to the air cooling zone side conveyor 3B. The structure is such that it is brought into an upright state again by the upright action of the stopper 4 and is allowed to pass through the air cooling chamber B.

この構成によつて加熱室8の出口開口部21の
開口面積を著しく縮少するとともに該出口開口部
21の上下に蓄圧室22,22を配設し、該蓄圧
室22,22から高温ガスを噴出せしめ該出口部
21における内外の空気の自由な流通を防止して
いる。したがつて加熱室8の空冷帯Bの開口部2
6あるいは外部からの低温空気の侵入が防止さ
れ、加熱室8の雰囲気の高温維持が達成される。
With this configuration, the opening area of the outlet opening 21 of the heating chamber 8 is significantly reduced, and pressure accumulators 22, 22 are arranged above and below the outlet opening 21, and high temperature gas is discharged from the pressure accumulators 22, 22. This prevents free flow of air between the inside and outside of the outlet section 21. Therefore, the opening 2 of the air cooling zone B of the heating chamber 8
6 or the intrusion of low-temperature air from the outside is prevented, and the atmosphere in the heating chamber 8 is maintained at a high temperature.

第3図は上記した作用を行なうためのフローシ
ートを例示しているものであり、このフローシー
トにもとづいてガスの流れを説明すると、排風機
10によつて排出された蒸発可燃ヒユーム含有の
加熱室8内の雰囲気は、該排風機10から熱交換
器27を経て脱臭装置28に送られ、バーナー2
9で燃焼脱臭されたのち再び熱交換器27内に導
入され、更に他の熱交換器30に導入される。そ
してこの熱交換器30内の高温ガスは送風機31
の作用によつて導管32内に送入され、該導管3
2から前記した蓄圧室22,22,23,23、
および二重構造の内壁15,16周壁18の空間
19,19内に導入され、該蓄圧室22,23の
ノズルから放出して出口開口部21および入口開
口部11における内外空気の流通を防止すると共
に内壁15,16および周壁18の表面温度を
180℃以上に保持させる。そして上記各空間19,
19内の高温ガスは排風機42によつて高温の儘
煙突33に送り入れ排出する。また熱交換器30
を通過する高温ガスの1部は、送風機31により
脱臭用バーナー29およびオーブン昇温用バーナ
ー34に送り入れ、それによつて燃焼空気を昇温
し燃費の節約を行なつている。35は排出される
可燃性ヒユームの対空気比検出装置であつて、排
気ガス内の可燃性ヒユームの混合比率を検出し、
混合比率の増減に対応して排風機10の回転を制
御して空気流入口36からの稀釈空気の導入量を
調整し、それによつて常時オーブン内雰囲気ガス
の可燃性ヒユームの濃度を爆発限界の下限以下に
なるよう作動している。上記したように受け渡し
室5および加熱室8の1部の内壁温度が180℃以
上に保たれているため内壁面へのヒユーム付着が
殆んどないこと、および加熱帯Aの出入口23,
11からの外気の流入が防止されていることから
塗装板材1から蒸発する可燃性ヒユーム量は検知
装置35によつてほぼ正確に検知でき、排風機1
0の回転制御、稀釈空気の導入量の増減が的確に
遂行され、安全操業が確保される。
FIG. 3 shows an example of a flow sheet for carrying out the above-mentioned action. Based on this flow sheet, the flow of gas is explained. The atmosphere inside the chamber 8 is sent from the exhaust fan 10 to the deodorizing device 28 via the heat exchanger 27, and then to the burner 2.
After being combusted and deodorized in step 9, it is introduced into the heat exchanger 27 again and then into another heat exchanger 30. The high temperature gas in the heat exchanger 30 is then transferred to the blower 31.
is fed into the conduit 32 by the action of the conduit 3
2 to 2 to the pressure accumulation chambers 22, 22, 23, 23,
and is introduced into the spaces 19, 19 of the double-structured inner walls 15, 16 and the surrounding wall 18, and is discharged from the nozzles of the pressure accumulating chambers 22, 23 to prevent circulation of internal and external air at the outlet opening 21 and the inlet opening 11. and the surface temperature of the inner walls 15, 16 and the peripheral wall 18.
Keep at 180℃ or higher. And each of the above spaces 19,
The high-temperature gas in the chimney 19 is sent to the high-temperature chimney 33 and discharged by the exhaust fan 42. Also, the heat exchanger 30
A part of the high-temperature gas passing through is sent to the deodorizing burner 29 and the oven temperature increasing burner 34 by the blower 31, thereby increasing the temperature of the combustion air and saving fuel consumption. 35 is a combustible fume to air ratio detection device that detects the mixture ratio of flammable fume in exhaust gas;
The rotation of the exhaust fan 10 is controlled in response to an increase or decrease in the mixing ratio, and the amount of diluted air introduced from the air inlet 36 is adjusted, thereby constantly keeping the concentration of flammable fumes in the oven atmospheric gas below the explosion limit. It operates so that it is below the lower limit. As mentioned above, since the inner wall temperature of a portion of the delivery chamber 5 and the heating chamber 8 is maintained at 180° C. or higher, there is almost no adhesion of fume to the inner wall surface, and the entrance and exit port 23 of the heating zone A,
Since the inflow of outside air from the exhaust fan 11 is prevented, the amount of flammable fume evaporating from the painted board material 1 can be almost accurately detected by the detection device 35.
0 rotation control and increase/decrease in the amount of dilution air introduced, ensuring safe operation.

(発明の効果) このように本発明の連続乾燥オーブンは、オー
ブンの加熱帯Aの受け渡し室5の内壁15と該受
け渡し室5と加熱室8との境界開口部12の近傍
の該加熱室8の内壁16および排気ダクト17の
内周壁18をそれぞれ空気流通可能な空間19,
19を介在せしめた2重構造となし、該空間1
9,19内に脱臭装置から出る高温ガスを導入し
て上記各内壁15,16および内周壁18の表面
温度を180℃以上に持続せしめるようになしてい
るから加熱室8から受け渡し室5を経て排気ダク
ト17に向う排ガスの移動域の内壁面に可燃性の
ヒユームの付着が防止され、加熱室8内において
塗装板材1から蒸発した可燃性ヒユームの殆んど
すべてが脱臭装置に導き入れられ、脱臭装置にお
ける燃焼に際してはこの可燃性ヒユームの熱カロ
リーを有効に利用することができ、また排気ダク
ト内での可燃性ヒユームの濃度測定の値が加熱室
8内での可燃性ヒユーム濃度とほぼ一致すること
になり、加熱室8内の雰囲気を爆発限界下限に制
御するために稀釈空気の導入を効果的に制御する
ことができる。
(Effects of the Invention) As described above, the continuous drying oven of the present invention has the inner wall 15 of the delivery chamber 5 of the heating zone A of the oven and the heating chamber 8 near the boundary opening 12 between the delivery chamber 5 and the heating chamber 8. The inner wall 16 of the exhaust duct 17 and the inner circumferential wall 18 of the exhaust duct 17 are respectively provided with a space 19 through which air can circulate.
It has a double structure with 19 interposed therebetween, and the space 1
High-temperature gas from the deodorizing device is introduced into the interiors of the heating chambers 8 and 19 to maintain the surface temperature of the inner walls 15, 16 and the inner circumferential wall 18 at 180°C or higher. Flammable fumes are prevented from adhering to the inner wall surface of the movement area of the exhaust gas toward the exhaust duct 17, and almost all of the flammable fumes evaporated from the painted plate material 1 in the heating chamber 8 are introduced into the deodorizing device. During combustion in the deodorizing device, the thermal calories of this flammable fume can be effectively used, and the value measured for the concentration of flammable fume in the exhaust duct almost matches the concentration of flammable fume in the heating chamber 8. Therefore, the introduction of dilution air can be effectively controlled in order to control the atmosphere within the heating chamber 8 to the lower explosive limit.

更に加熱帯Aと空冷帯Bとを実質的に分離して
該加熱帯Aおよび該空冷帯Bのそれぞれに支持捍
4a,4bを備えた加熱帯側コンベヤー3Aおよ
び受止捍4を備えた冷却帯側コンベヤー3Bを設
けるとともに両コンベヤー3A,3B間に板材1
を水平状態となして移送する中間搬送コンベヤー
20を設けて加熱帯Aと空冷帯Bとの接続部の開
口部21,26の開口面積を縮少し、該加熱帯A
の出入口に蓄圧室22,22および23,23を
対向配設しているから、加熱帯Aの板材1の出入
口における空気の流通が実質的に防止され、低温
空気が加熱室8内に流入しなくなるため熱損失が
少なくなり、僅かな焚量でもつて加熱室1の高温
維持が可能となつて飛躍的な省エネルギーを達成
することができる。
Further, the heating zone A and the air cooling zone B are substantially separated, and each of the heating zone A and the air cooling zone B is provided with a heating zone side conveyor 3A and a receiving tube 4, respectively. A belt side conveyor 3B is provided, and a plate material 1 is installed between both conveyors 3A and 3B.
An intermediate conveyor 20 is provided to transport the heating zone A and the air cooling zone B in a horizontal state to reduce the opening areas of the openings 21 and 26 at the connection between the heating zone A and the air cooling zone B.
Since the pressure accumulating chambers 22, 22 and 23, 23 are disposed facing each other at the entrance and exit of the heating zone A, air circulation at the entrance and exit of the plate material 1 of the heating zone A is substantially prevented, and low-temperature air flows into the heating chamber 8. This reduces heat loss, making it possible to maintain a high temperature in the heating chamber 1 even with a small amount of combustion, and achieving dramatic energy savings.

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

第1図は本発明の乾燥オーブンを例示した側面
断面図、第2図は第1図のA−A正面断面図、第
3図は本発明乾燥オーブンのフローシート説明
図、そして第4図は従来の乾燥オーブンの側面断
面図、第5図は第4図のA−A線正面断面図であ
る。 A……加熱帯、B……空冷帯、1……塗装板
材、2……搬送コンベヤー、3A……1対の支持
捍を備えた加熱帯側コンベヤー、3B……支持捍
を備えた冷却帯側コンベヤー、4……支持捍、4
a,4b……1対の支持捍、5……受け渡し室、
8……加熱室、11……入口開口部、12……受
け渡し室と加熱室との境界開口部、15……受け
渡し室の内壁、16……境界開口部近傍の加熱室
の内壁、17……排気ダクト、18……排気ダク
トの内周壁、19……空間、20……中間搬送コ
ンベヤー、21……出口開口部、22,23……
蓄圧室。
FIG. 1 is a side sectional view illustrating the drying oven of the present invention, FIG. 2 is a front sectional view taken along line AA in FIG. FIG. 5 is a side sectional view of a conventional drying oven, and FIG. 5 is a front sectional view taken along the line A--A in FIG. A... Heating zone, B... Air cooling zone, 1... Painted plate material, 2... Conveyor, 3A... Heating zone side conveyor equipped with a pair of support strips, 3B... Cooling zone equipped with support strips. Side conveyor, 4...Supporting rack, 4
a, 4b...a pair of support racks, 5...transfer room,
8... Heating chamber, 11... Inlet opening, 12... Boundary opening between delivery chamber and heating chamber, 15... Inner wall of delivery chamber, 16... Inner wall of heating chamber near boundary opening, 17... ...Exhaust duct, 18...Inner peripheral wall of exhaust duct, 19...Space, 20...Intermediate conveyor, 21...Exit opening, 22, 23...
Pressure accumulation chamber.

Claims (1)

【特許請求の範囲】[Claims] 1 オーブンの加熱帯Aの受け渡し室5の内壁1
5と該受け渡し室5と加熱室8との境界開口部1
2の近傍の該加熱室8の内壁16および排気ダク
ト17の内周壁18をそれぞれ空気流通可能な空
間19,19を介在せしめた2重構造となし、該
空間19,19内に脱臭装置から出る高温ガスを
導入して上記各内壁15,16および内周壁18
の表面温度を180℃以上に持続せしめるようにな
し、更に加熱帯Aと空冷帯Bとを実質的に分離し
て該加熱帯Aおよび該空冷帯Bのそれぞれに1対
の支持捍4a,4bを備えた加熱帯側コンベヤー
3Aおよび受止捍4を備えた冷却帯側コンベヤー
3Bを設けるとともに、両コンベヤー3A,3B
間に板材1を水平状態となして移送する中間搬送
コンベヤー20を設けて加熱帯Aと空冷帯Bとの
接続開口部21,26の開口面積を縮小し、該加
熱帯Aの出入口に上下一対の蓄圧室22,22お
よび23,23を対向配設したことを特徴とする
連続乾燥オーブン。
1 Inner wall 1 of delivery chamber 5 of heating zone A of oven
5 and the boundary opening 1 between the delivery chamber 5 and the heating chamber 8
The inner wall 16 of the heating chamber 8 and the inner circumferential wall 18 of the exhaust duct 17 in the vicinity of No. 2 have a double structure with spaces 19, 19 through which air can flow, respectively, and the deodorizing device exits into the spaces 19, 19. Each of the inner walls 15, 16 and the inner peripheral wall 18 are heated by introducing high temperature gas.
The heating zone A and the air cooling zone B are substantially separated, and each of the heating zone A and the air cooling zone B is provided with a pair of support plates 4a and 4b. A heating zone side conveyor 3A equipped with a cooling zone side conveyor 3B equipped with a catch plate 4 is provided, and both conveyors 3A, 3B are provided.
An intermediate conveyor 20 for horizontally transporting the plate material 1 is provided in between to reduce the opening area of the connecting openings 21 and 26 between the heating zone A and the air cooling zone B, and a pair of upper and lower openings are provided at the entrance and exit of the heating zone A. A continuous drying oven characterized in that pressure accumulation chambers 22, 22 and 23, 23 are arranged facing each other.
JP19097784A 1984-09-12 1984-09-12 Continuous drying oven Granted JPS6170375A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19097784A JPS6170375A (en) 1984-09-12 1984-09-12 Continuous drying oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19097784A JPS6170375A (en) 1984-09-12 1984-09-12 Continuous drying oven

Publications (2)

Publication Number Publication Date
JPS6170375A JPS6170375A (en) 1986-04-11
JPH0457386B2 true JPH0457386B2 (en) 1992-09-11

Family

ID=16266815

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19097784A Granted JPS6170375A (en) 1984-09-12 1984-09-12 Continuous drying oven

Country Status (1)

Country Link
JP (1) JPS6170375A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5827825U (en) * 1981-08-17 1983-02-23 東芝熱器具株式会社 rotary switch

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5827825U (en) * 1981-08-17 1983-02-23 東芝熱器具株式会社 rotary switch

Also Published As

Publication number Publication date
JPS6170375A (en) 1986-04-11

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