JPH0810679A - Coating drying device - Google Patents

Coating drying device

Info

Publication number
JPH0810679A
JPH0810679A JP14752394A JP14752394A JPH0810679A JP H0810679 A JPH0810679 A JP H0810679A JP 14752394 A JP14752394 A JP 14752394A JP 14752394 A JP14752394 A JP 14752394A JP H0810679 A JPH0810679 A JP H0810679A
Authority
JP
Japan
Prior art keywords
heat
furnace
coating
hot air
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.)
Pending
Application number
JP14752394A
Other languages
Japanese (ja)
Inventor
Hideaki Nakadokoro
所 英 明 中
Michio Taniguchi
口 道 夫 谷
Shinji Tomitaka
高 晋 二 冨
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.)
Trinity Industrial Corp
Original Assignee
Trinity Industrial 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 Trinity Industrial Corp filed Critical Trinity Industrial Corp
Priority to JP14752394A priority Critical patent/JPH0810679A/en
Publication of JPH0810679A publication Critical patent/JPH0810679A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To reduce equipment cost by miniaturizing a heat medium oil heating boiler which serves as a heat source for a hot blast circulation type tunnel furnace of a heat medium oil indirect heating system to such an extent that a furnace interior is maintained at an actual use temperature, and at the same time, enable even a small-sized heating boiler to increase an intra-furnace temperature to the actual use temperature in a time almost equivalent to that required for heating by a conventional heating boiler. CONSTITUTION:Heat medium oil circulation piping 12 which feeds by circulation a heat medium oil heated by the heat discharged by a power generation device 16 which generates an electric power as an emergency power supply for coating facilities, is connected to a heat exchanger 8 interposed in a hot blast circulation passage 11 for feeding a hot blast by circulation into a tunnel furnace 3. In addition, closable doors 4, 4 which block the inlet and outlet 2, 2 of the tunnel furnace 3 when a coating drying device stops are formed at the inlet and outlet 2, 2. Further, in the hot blast circulation passage 11, a bypass 18 with an interposed heat retaining fan 17 for blowing an air heated by the hat released by the heat exchanger 8 when the coating drying device stops, is formed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、コンベアで連続的に搬
送される自動車ボディ等の塗膜を乾燥させる熱風循環式
のトンネル形炉を用いた塗装乾燥装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coating dryer using a hot air circulation type tunnel furnace for drying coating films on automobile bodies or the like which are continuously conveyed by a conveyor.

【0002】[0002]

【従来の技術】例えば、自動車ボディの塗膜を乾燥させ
る塗装乾燥装置のトンネル形炉には、炉内からリターン
ダクトを通じて吸引した熱風を使用温度に加熱してサプ
ライダクトから再び炉内に導入する熱風循環経路が形成
されている。そして、熱風を使用温度に加熱する熱源の
違いにより、熱風循環経路に介装された熱交換器に高温
の熱媒油を供給してその熱交換器により熱風を間接加熱
する熱媒油間接加熱方式と、熱風循環経路に介装された
熱交換器に高温の燃焼ガスを供給してその熱交換器によ
り熱風を間接加熱する燃焼ガス間接加熱方式と、熱風循
環経路に介装されたバーナで熱風を直接加熱するように
なされた燃焼ガス直接加熱方式とがある。
2. Description of the Related Art For example, in a tunnel furnace of a coating dryer for drying a coating film on an automobile body, hot air sucked through a return duct from inside the furnace is heated to a working temperature and introduced into the furnace again from a supply duct. A hot air circulation path is formed. Then, due to the difference in the heat source that heats the hot air to the operating temperature, the high-temperature heat medium oil is supplied to the heat exchanger interposed in the hot air circulation path, and the heat medium is indirectly heated by the heat exchanger. Method, a combustion gas indirect heating method in which high-temperature combustion gas is supplied to the heat exchanger installed in the hot air circulation path to indirectly heat the hot air by the heat exchanger, and a burner installed in the hot air circulation path. There is a combustion gas direct heating system designed to directly heat hot air.

【0003】ところで、自動車ボディの塗膜乾燥用のト
ンネル形炉は、その長さが数十〜百数十メートルもある
ので、炉内の温度分布を均一にするために、あるいは所
要の温度分布を得るために、トンネル形炉をその長手方
向に沿って複数のゾーンに分割して各ゾーンごとに熱風
循環経路を形成すると、燃焼ガス間接加熱方式及び燃焼
ガス直接加熱方式の場合、各熱風循環経路ごとにバーナ
が必要となり、集中管理しにくくメンテナンス要員も大
勢必要となる。
By the way, since a tunnel furnace for drying a coating film of an automobile body has a length of several tens to hundreds of tens of meters, a temperature distribution required for uniform temperature distribution in the furnace or a required temperature distribution. In order to obtain the above, if the tunnel furnace is divided into multiple zones along its longitudinal direction and hot air circulation paths are formed in each zone, in the case of the combustion gas indirect heating method and the combustion gas direct heating method, each hot air circulation A burner is required for each route, it is difficult to centrally manage, and many maintenance personnel are required.

【0004】これに対し、熱媒油間接加熱方式は、熱媒
油加熱ボイラで高温に加熱した熱媒油を各熱交換器に循
環供給すれば足りるので、各ゾーンごとの付帯設備が簡
素化されるだけでなく、塗装工場で複数のラインが形成
されている場合に各ラインごとにトンネル形炉を設置し
ても熱媒油ボイラは一基で済み、そのメンテナンスが容
易になるだけでなく、各ゾーンの熱交換器の寿命が長
い、火災の危険がない、温度調節が容易、集中管理が可
能になるというメリットがある。
On the other hand, in the heat transfer oil indirect heating method, it is sufficient to circulate and supply the heat transfer oil heated to a high temperature in the heat transfer oil heating boiler to each heat exchanger, so that the auxiliary equipment for each zone is simplified. In addition, if multiple lines are formed in the coating plant, even if a tunnel furnace is installed for each line, only one heat transfer oil boiler is required, which not only facilitates maintenance. The advantages are that the life of the heat exchanger in each zone is long, there is no risk of fire, temperature control is easy, and centralized control is possible.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、熱媒油
間接加熱方式によりトンネル形炉内を加熱する場合、炉
内温度が一旦使用温度まで昇温された後は使用温度を維
持するのにそれ程多くの熱量を必要としないものの、長
時間運転休止して炉内温度が低下した後に運転を再開す
るとトンネル形炉の各ゾーンを使用温度まで所定時間内
に一斉に昇温させるのに非常に多くの熱量を必要とし、
このときに必要な熱量に応じて熱媒油加熱ボイラを設計
しなければないので、加熱ボイラは大型化し、設備費が
嵩むという問題があった。
However, in the case of heating the inside of the tunnel type furnace by the heating medium oil indirect heating method, the temperature inside the furnace is once increased to the working temperature, and so much is needed to maintain the working temperature. Although it does not require the amount of heat of the furnace, if the operation is restarted after the temperature inside the furnace has dropped for a long time after the operation has been stopped for a long time, a large amount of Requires heat,
At this time, the heating oil heating boiler must be designed in accordance with the amount of heat required, so that there is a problem that the heating boiler becomes large and the equipment cost increases.

【0006】すなわち、運転時間のほとんどは炉内を使
用温度に維持できる程度の比較的少ない熱量を供給でき
れば足りるにもかかわらず、室温まで下がった炉内温度
を所定時間内に使用温度に昇温するためにその間だけは
大型の加熱ボイラをフルパワーで運転しなければならな
いので、小型の加熱ボイラを用いることができなかっ
た。そこで、本発明は、トンネル形炉を使用温度に維持
できる程度の小型の加熱ボイラを使用して設備費を軽減
すると同時に、小型の加熱ボイラでも、従来と同程度の
時間で炉内を使用温度まで昇温することができるように
することを技術的課題としている。
That is, most of the operating time is sufficient if a relatively small amount of heat capable of maintaining the inside of the furnace at the working temperature can be supplied, but the temperature inside the furnace lowered to room temperature is raised to the working temperature within a predetermined time. In order to do so, a large heating boiler must be operated at full power only during that time, so it was not possible to use a small heating boiler. Therefore, the present invention reduces the facility cost by using a small heating boiler that can maintain the tunnel furnace at the operating temperature, and at the same time, even for a small heating boiler, the operating temperature in the furnace can be kept in the same time as the conventional one. The technical issue is to be able to raise the temperature up to.

【0007】[0007]

【課題を解決するための手段】この課題を解決するため
に、本願第一の発明は、両端に出入口を開口したトンネ
ル形炉に、その炉内からリターンダクトを通じて吸引し
た熱風を熱交換器から供与される熱で使用温度に加熱し
てサプライダクトから再び炉内に導入する熱風循環ファ
ンを介装した熱風循環経路が設けられた塗装乾燥装置に
おいて、前記熱交換器に、塗装設備の非常用電源となる
電力を発生する発電装置の排熱によって加熱された熱媒
油を循環供給する熱媒油循環配管が接続され、前記トン
ネル形炉の出入口には、その出入口を塗装乾燥装置の運
転休止時に閉塞する開閉扉が設けられ、前記熱風循環経
路には、塗装乾燥装置の運転休止時に前記熱交換器が放
出する熱で加熱された空気を前記トンネル形炉の炉内に
送風する保温ファンを介装したバイパス路が形成されて
いることを特徴とする。
In order to solve this problem, the first invention of the present application is directed to a tunnel furnace having openings at both ends, and hot air sucked from the inside of the furnace through a return duct from a heat exchanger. In a coating dryer equipped with a hot-air circulation path that has a hot-air circulation fan that heats up to the operating temperature with the supplied heat and then reintroduces it from the supply duct into the furnace, use the heat exchanger as an emergency for coating equipment. A heat transfer oil circulation pipe that circulates and supplies heat transfer oil heated by the exhaust heat of a power generator that generates electric power to be used as a power source is connected to the entrance of the tunnel furnace and the operation of the coating dryer is stopped. An opening / closing door that is closed at times is provided, and the hot air circulation path blows air heated by the heat released by the heat exchanger into the furnace of the tunnel furnace in the hot air circulation path. Wherein the bypass passage is formed that interposed.

【0008】また、本願第二の発明は、前記保温ファン
を介装したバイパス路を形成することに代えて、塗装乾
燥装置の運転休止時に前記熱交換器が放出する熱で加熱
された空気を前記トンネル形炉の炉内に送風し得る程度
の小風量で前記熱風循環ファンを稼動させる制御装置を
備えたことを特徴とする。
Further, in the second invention of the present application, instead of forming the bypass passage in which the heat insulating fan is interposed, the air heated by the heat released by the heat exchanger when the coating drying apparatus is stopped is operated. It is characterized by comprising a control device for operating the hot air circulation fan with a small amount of air that can be blown into the furnace of the tunnel furnace.

【0009】[0009]

【作用】本発明によれば、通常運転の際には、高温に加
熱された熱媒油を熱交換器に供給すると共に、熱風循環
経路に介装された熱風循環ファンを運転することによ
り、炉内からリターンダクトを介して吸引された熱風と
高温の熱媒油との間で熱交換され、熱風が使用温度まで
加熱されて再び炉内に供給される。このとき、リターン
ダクトを介して吸引される熱風は使用温度に近い高温な
ので、熱媒油を介して供給する熱量もわずかで足り、し
たがって熱媒油加熱ボイラは小型のもので足りる。
According to the present invention, during normal operation, the heat transfer oil heated to a high temperature is supplied to the heat exchanger, and the hot air circulation fan installed in the hot air circulation path is operated, Heat is exchanged between the hot air sucked from the inside of the furnace through the return duct and the high-temperature heat transfer oil, the hot air is heated to the working temperature, and the hot air is supplied again into the furnace. At this time, since the hot air sucked through the return duct is at a high temperature close to the operating temperature, the amount of heat supplied via the heat transfer oil is also small, and therefore the heat transfer oil heating boiler can be small in size.

【0010】そして、乾燥装置の運転が終了すると、熱
風循環ファンが停止されると共に、トンネル形炉の出入
口に配設された開閉扉が閉塞され、高温空気が炉内に閉
じ込めらる。したがって、炉内外の空気の出入りがなく
なり、炉内の温度が炉外に逃げ難くくなる。
When the operation of the drying device is completed, the hot air circulation fan is stopped and the opening / closing door arranged at the entrance / exit of the tunnel furnace is closed, so that high temperature air is trapped in the furnace. Therefore, the air in and out of the furnace is prevented from flowing in and out, and the temperature in the furnace becomes difficult to escape to the outside of the furnace.

【0011】また、塗装設備の非常用電源となる電力を
発生する発電装置は非常時に備えてほとんど休みなく稼
動されており、その発電装置が異常加熱されないように
発電装置の排熱で加熱された熱媒油を循環供給する熱媒
油循環配管が、熱風循環炉に介装された熱交換器に接続
されているので、熱交換器にはわずかな熱量が常に供給
されている。
In addition, the power generator for generating electric power, which serves as an emergency power source for the coating equipment, is operated almost without a break in case of emergency, and is heated by the exhaust heat of the power generator so as not to be abnormally heated. Since the heat medium oil circulation pipe for circulating and supplying the heat medium oil is connected to the heat exchanger interposed in the hot air circulation furnace, a small amount of heat is always supplied to the heat exchanger.

【0012】したがって、熱風循環経路に形成されたバ
イパス路の保温ファンが稼動されると、前記熱交換器が
放出する熱で加熱された空気が前記トンネル形炉の炉内
に送風されて、炉内温度が使用温度より下がったとして
も室温までは低下することがないので、運転再開時には
供給熱量が少なくても短時間で炉内を使用温度まで加熱
することができる。
Therefore, when the heat insulation fan of the bypass passage formed in the hot air circulation passage is operated, the air heated by the heat released by the heat exchanger is blown into the furnace of the tunnel furnace, and the furnace is heated. Even if the internal temperature falls below the operating temperature, it does not fall to room temperature, so that the furnace can be heated to the operating temperature in a short time when the amount of heat supplied is small when the operation is restarted.

【0013】[0013]

【実施例】以下、本発明を図面に示す実施例に基づいて
具体的に説明する。図1は本発明に係る塗装乾燥装置を
示すフローシート、図2はそのタイムチャート、図3は
他の実施例を示すタイムチャートである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below based on embodiments shown in the drawings. 1 is a flow sheet showing a coating and drying apparatus according to the present invention, FIG. 2 is a time chart thereof, and FIG. 3 is a time chart showing another embodiment.

【0014】本例の塗装乾燥装置1は、両端に出入口
2,2を開口した複数のトンネル形炉3,3・・・を有
し、その出入口2,2には当該塗装乾燥装置1の運転休
止時に出入口2,2を閉塞する開閉扉4,4が設けられ
ている。また、各トンネル形炉3は夫々複数のゾーンに
分割され、入口側に輻射パネル5が配された輻射加熱ゾ
ーン5が形成され、その後段側には熱風をワークに直接
吹き付ける対流加熱ゾーン6が形成されている。
The coating / drying apparatus 1 of this example has a plurality of tunnel furnaces 3, 3 ... Opening the inlets / outlets 2 and 2 at both ends, and operating the coating / drying apparatus 1 at the inlets / outlets 2 and 2. Opening / closing doors 4 and 4 are provided to close the entrances and exits 2 and 2 at rest. Further, each tunnel furnace 3 is divided into a plurality of zones, and a radiant heating zone 5 in which a radiant panel 5 is arranged is formed on the inlet side, and a convection heating zone 6 for blowing hot air directly onto the work is formed on the subsequent stage side. Has been formed.

【0015】各ゾーン5,6には、その炉内からリター
ンダクト7を通じて吸引した熱風を熱交換器8から供与
される熱で使用温度に加熱してサプライダクト9から再
び炉内に導入する熱風循環ファン10を介装した熱風循
環経路11が設けられている。前記熱風循環経路11に
介装された熱交換器8には、加熱された熱媒油を間断な
く循環供給する熱媒油循環配管12が接続され、当該熱
媒油循環配管12には、熱媒油加熱ボイラ13が介装さ
れている。熱媒油加熱ボイラ13は、熱交換器14を介
して熱媒油を加熱する燃焼室15を備えており、また、
前記熱交換器14には、塗装設備の非常用電源となる電
力を発生する発電装置16の排熱が回収されるように成
されている。そして、燃焼室15及び発電装置16で発
生する熱を、熱交換器14を介して熱媒油に供与し、少
なくとも炉内を所定の使用温度に加熱できる程度の温度
に加熱するように成されている。
In each of the zones 5 and 6, the hot air sucked from the inside of the furnace through the return duct 7 is heated to the working temperature by the heat supplied from the heat exchanger 8 and introduced into the furnace from the supply duct 9 again. A hot air circulation path 11 having a circulation fan 10 interposed therein is provided. The heat exchanger 8 installed in the hot air circulation path 11 is connected to a heat medium oil circulation pipe 12 that circulates the heated heat medium oil without interruption, and the heat medium oil circulation pipe 12 is connected to the heat medium oil circulation pipe 12. A medium oil heating boiler 13 is interposed. The heat transfer oil heating boiler 13 includes a combustion chamber 15 that heats the heat transfer oil via the heat exchanger 14, and
The heat exchanger 14 is configured to recover the exhaust heat of a power generator 16 that generates electric power that serves as an emergency power source for coating equipment. Then, the heat generated in the combustion chamber 15 and the power generator 16 is supplied to the heat transfer oil via the heat exchanger 14 to heat at least the temperature in the furnace to a predetermined working temperature. ing.

【0016】また、熱風循環経路11には、塗装乾燥装
置1の運転休止時に熱交換器8が放出する熱で加熱され
た空気を前記トンネル形炉3の炉内に送風する保温ファ
ン17を介装したバイパス路18が形成されている。こ
の保温ファン17は、熱風循環ファン10に比して風量
が少ない小型のものが用いられており、制御装置19の
制御信号によりオン・オフ制御される。この制御装置1
9には、トンネル形炉3内の雰囲気温度を検出する温度
センサ20が接続され、当該センサ20により検出され
た雰囲気温度が予め設定された所定の温度以下になった
時に、保温ファン17を稼動するスイッチ信号を出力す
るように成されている。
In addition, the hot air circulation path 11 is provided with a heat insulating fan 17 for blowing air heated by the heat emitted from the heat exchanger 8 into the furnace of the tunnel furnace 3 when the coating drying apparatus 1 is out of operation. A mounted bypass passage 18 is formed. As the heat insulation fan 17, a small one having a smaller air volume than the hot air circulation fan 10 is used, and the heat insulation fan 17 is on / off controlled by a control signal of the control device 19. This control device 1
A temperature sensor 20 for detecting the ambient temperature in the tunnel furnace 3 is connected to 9 and the heat insulation fan 17 is operated when the ambient temperature detected by the sensor 20 falls below a preset predetermined temperature. The switch signal is output.

【0017】以上が本発明の一例構成であって、次に、
その作用について説明する。まず、自動車ボディを乾燥
するときは、熱媒油循環配管12を介して還流されてき
た熱媒油が、熱交換器14で燃焼室15及び発電装置1
6で生じた熱で高温に加熱されて、各トンネル形炉3に
配設された熱交換器8に送給される。このように、熱媒
油加熱ボイラ13は、燃焼室15だけなく発電装置16
の排熱も熱源としているので、その分、小型化すること
ができる。
The above is an example configuration of the present invention.
The operation will be described. First, when the automobile body is dried, the heat transfer oil that has recirculated through the heat transfer oil circulation pipe 12 is transferred to the combustion chamber 15 and the power generation device 1 in the heat exchanger 14.
It is heated to a high temperature by the heat generated in 6 and sent to the heat exchanger 8 arranged in each tunnel furnace 3. As described above, the heating oil heating boiler 13 includes the power generation device 16 as well as the combustion chamber 15.
Since the exhaust heat of is also used as a heat source, the size can be reduced accordingly.

【0018】次いで、高温に加熱された熱媒油が、各ト
ンネル形炉3の熱風循環経路11に介装された熱交換器
8,8・・・に送給され、熱風循環ファン10によりト
ンネル形炉3内からリターンダクト7を介して吸引され
た熱風と熱媒油との間で熱交換が行われ、使用温度に加
熱される。そして、熱風循環ファン10により再びサプ
ライダクト9を介してトンネル形炉3に送給され、炉内
が前記使用温度(例えは 150℃)に維持され、一定の品
質で塗膜が乾燥される。
Next, the heat transfer oil heated to a high temperature is fed to the heat exchangers 8, 8 ... Which are provided in the hot air circulation path 11 of each tunnel furnace 3, and the hot air circulation fan 10 tunnels the heat exchanger oil. Heat exchange is performed between the hot air sucked from the inside of the furnace 3 through the return duct 7 and the heat transfer oil, and is heated to the operating temperature. Then, the hot air circulation fan 10 feeds the gas again to the tunnel furnace 3 through the supply duct 9, the inside of the furnace is maintained at the working temperature (for example, 150 ° C.), and the coating film is dried with a constant quality.

【0019】そして、一日の作業が終了すると、熱風循
環ファン10及び熱媒油加熱ボイラ13の運転を停止す
ると同時に、各トンネル形炉3の温度が下がる前に夫々
の出入口2,2に配設された開閉扉4,4を閉塞する。
(図2:T0 )。これにより、炉内外の空気の出入りが
なくなり、熱空気が炉外に流出したり、冷たい外気が炉
内に侵入したりすることがないので、炉内温度は急激に
低下することなく、極めてゆっくりと低下する。なお、
塗装乾燥装置1の運転を停止しても、塗装設備の非常用
電源となる電力を発生する発電装置16はほとんど休み
なく運転されているので、熱媒油には熱交換器15を介
してその排熱が供与される。
When the work of one day is completed, the hot air circulation fan 10 and the heat medium oil heating boiler 13 are stopped, and at the same time, the hot air circulating fan 10 and the heat transfer oil heating boiler 13 are distributed to the respective inlets and outlets 2 and 2 before the temperature of each tunnel furnace 3 is lowered. The opening / closing doors 4 and 4 provided are closed.
(FIG. 2: T 0 ). As a result, the air inside and outside the furnace does not come in and out, hot air does not flow out of the furnace, and cold outside air does not enter the furnace.Therefore, the temperature inside the furnace does not drop sharply and is extremely slow. And decline. In addition,
Even if the operation of the coating / drying apparatus 1 is stopped, the power generator 16 that generates electric power as an emergency power source for the coating equipment is operated almost without interruption, so that the heat transfer oil is transferred to the heat transfer oil via the heat exchanger 15. Exhaust heat is provided.

【0020】そして、各トンネル形炉3の炉内温度は、
夫々の温度センサ20でモニタされ、予め設定された所
定温度(例えば80℃)以下に下がると、制御装置19
からそのトンネル形炉3の熱風循環経路11に設けられ
たバイパス路18の保温ファン17を起動するスイッチ
信号が出力される(図2:T1 )。保温ファン17が回
転されると、炉内の空気がリターンダクト7から吸引さ
れ、熱交換器8により熱媒油と熱交換が行われ、加熱さ
れた空気がサプライダクト9を介して炉内に送給される
ので、炉内温度が上昇する。
The temperature inside each tunnel furnace 3 is
When the temperature is monitored by each temperature sensor 20 and drops below a preset predetermined temperature (for example, 80 ° C.), the control device 19
Outputs a switch signal for activating the heat insulation fan 17 in the bypass 18 provided in the hot air circulation path 11 of the tunnel furnace 3 (FIG. 2: T 1 ). When the heat insulation fan 17 is rotated, the air in the furnace is sucked from the return duct 7, heat is exchanged with the heat transfer oil by the heat exchanger 8, and the heated air is introduced into the furnace through the supply duct 9. As it is delivered, the temperature inside the furnace rises.

【0021】次いで、温度センサ20で検出された炉内
温度が予め設定された温度(例えば80℃)に達する
と、熱風循環ファン10の回転が停止され(図2:
2 )、これを繰り返しながら、炉内温度を約80℃の
保温温度に維持する。このとき、熱媒油循環配管12を
循環する熱媒油には、発電装置16の排熱により各トン
ネル形炉3の炉内を使用温度より低い所定の温度(例え
ば80℃)に保温できる程度の熱が供与されており、ま
た、保温ファン17の送風量は熱風循環ファン10に比
して少ないので熱風循環経路11を循環する風量が少な
くなり、熱交換器8を介して熱媒油の熱を必要以上に奪
うこともなく、炉内は適温に保温される。
Next, when the temperature inside the furnace detected by the temperature sensor 20 reaches a preset temperature (for example, 80 ° C.), the rotation of the hot air circulation fan 10 is stopped (FIG. 2:
T 2 ), while repeating this, the temperature in the furnace is maintained at a heat retention temperature of about 80 ° C. At this time, the heat transfer oil circulating in the heat transfer oil circulation pipe 12 can be kept at a predetermined temperature (for example, 80 ° C.) lower than the working temperature by the exhaust heat of the power generation device 16 Since the amount of air blown by the heat insulation fan 17 is smaller than that of the hot air circulation fan 10, the amount of air circulated in the hot air circulation path 11 is small, and the heat transfer oil of the heat transfer oil is passed through the heat exchanger 8. The inside of the furnace is maintained at an appropriate temperature without taking heat more than necessary.

【0022】そして、塗装乾燥炉1の運転を再開すると
きは、保温ファン17を停止すると同時に熱媒油加熱ボ
イラ13と熱風循環ファン10を起動させて、各トンネ
ル形炉3の炉内を所定の使用温度(例えば 150℃) まで
昇温する(図2:T3 〜T4)。このとき炉内は80℃
に保温されているので、80℃から150℃まで昇温す
れば足り、一定時間内に昇温するのであれば、室温から
使用温度まで加熱する場合に比して少ない熱量で昇温す
ることができ、したがって、熱媒油加熱ボイラ13を小
型にすることができる。そして、炉内が所定の使用温度
に達した後、出入口2,2の開閉扉4,4を開いてワー
クを搬入する。
When the operation of the coating drying furnace 1 is restarted, the heat insulating fan 17 is stopped and at the same time, the heating medium oil heating boiler 13 and the hot air circulating fan 10 are started to make the inside of each tunnel furnace 3 predetermined. the temperature is raised to a use temperature (e.g., 0.99 ° C.) (FIG. 2: T 3 ~T 4). At this time, the temperature inside the furnace is 80 ℃
Since it is kept warm at 80 ° C, it is sufficient to raise the temperature from 80 ° C to 150 ° C, and if the temperature is raised within a certain period of time, it is possible to raise the temperature with a smaller amount of heat than when heating from room temperature to the operating temperature. Therefore, the heating oil heating boiler 13 can be downsized. Then, after the inside of the furnace reaches a predetermined operating temperature, the opening and closing doors 4 and 4 of the entrances and exits 2 and 2 are opened to carry in the work.

【0023】なお、温度センサ20はトンネル形炉3ご
とに設ける場合に限らず、各加熱ゾーン5,6ごとに設
けて、各ゾーン5,6ごとに個別に保温ファン17を運
転する場合であってもよい。また、トンネル形炉3の各
ゾーン5,6ごとに熱風循環経路11が形成された場合
について説明したが、各トンネル形炉3に一つの熱風循
環経路11しか形成されていない場合であってもよい。
The temperature sensor 20 is not limited to the case of being provided for each tunnel furnace 3, but may be provided for each of the heating zones 5 and 6 and the heat insulating fan 17 is operated individually for each of the zones 5 and 6. May be. Further, the case where the hot air circulation path 11 is formed for each of the zones 5 and 6 of the tunnel furnace 3 has been described, but even when only one hot air circulation path 11 is formed for each tunnel furnace 3. Good.

【0024】図3は他の実施例を示すタイムチャートで
ある。本例では、温度センサ20を設置する替わりに、
制御装置19にタイマーを内蔵し、塗装乾燥装置1の運
転を再開する一定時間前にタイマーからスイッチ信号が
出力されたときに保温ファン17を稼動開始させる制御
信号を出力するように成されている。
FIG. 3 is a time chart showing another embodiment. In this example, instead of installing the temperature sensor 20,
The control device 19 has a built-in timer, and is configured to output a control signal for starting the operation of the heat insulation fan 17 when a switch signal is output from the timer a predetermined time before the operation of the coating drying apparatus 1 is restarted. .

【0025】これは、運転休止時に炉内が常時一定温度
に保温されていなくても、運転再開時に炉内が室温より
高い約80℃の保温温度に昇温されていれば、先の実施
例と同様に、短時間で各トンネル形炉3の炉内を所定の
使用温度(例えば 150℃) まで昇温できることに着目し
たものである。ただし、発電装置16の排熱の熱量はそ
れほど多くはなく、炉内が室温まで下がったときに保温
温度まで昇温するのに長時間かかるので、本例では、制
御装置19に運転再開時(例えば、午前8時30分)を
予め設定しておき、例えばその3時間前から保温ファン
17を起動させるようになされている。
This means that even if the inside of the furnace is not always kept at a constant temperature when the operation is stopped, if the inside of the furnace is heated to a keeping temperature of about 80 ° C. which is higher than room temperature when the operation is restarted, Similarly to the above, the present invention focuses on the fact that the inside of each tunnel furnace 3 can be heated to a predetermined operating temperature (for example, 150 ° C.). However, the heat quantity of the exhaust heat of the power generation device 16 is not so large, and it takes a long time to raise the temperature to the heat retention temperature when the temperature inside the furnace falls to room temperature. For example, 8:30 am) is set in advance, and the heat insulating fan 17 is started, for example, 3 hours before that.

【0026】まず、一日の作業が終了すると、熱風循環
ファン10及び熱媒油加熱ボイラ13の運転を停止する
と同時に、各トンネル形炉3の出入口2,2に配設され
た開閉扉4,4を閉塞する。(図3:T0 )。そして、
炉内温度は徐々に低下し、運転再開時(例えば、午前8
時30分)の3時間前(午前5時30分)になると、タ
イマ20から出力されるスイッチ信号に基づいて制御装
置19から保温ファン17を起動させる制御信号が出力
される(図3:T1 )。
First, when the work of one day is completed, the hot air circulating fan 10 and the heat medium oil heating boiler 13 are stopped, and at the same time, the opening / closing doors 4, 4 arranged at the entrances / outlets 2, 2 of each tunnel furnace 3. Block 4 (FIG. 3: T 0 ). And
The temperature inside the furnace gradually decreases, and when the operation is restarted (for example, 8 am
At 3 hours before (hour 30 minutes) (5:30 am), a control signal for starting the heat insulation fan 17 is output from the control device 19 based on the switch signal output from the timer 20 (FIG. 3: T). 1 ).

【0027】これにより、炉内の空気が保温ファン17
によりリターンダクト7から吸引され、熱交換器8によ
り熱媒油と熱交換が行われ、加熱された空気がサプライ
ダクト9を介して炉内に送給されて、炉内温度が徐々に
上昇する。そして、塗装乾燥装置1の運転再開時(午前
8時30分)には、炉内温度が予め設定された温度(例
えば80℃)に達し、ここで熱媒油加熱ボイラ13及び
熱風循環ファン10が起動させると、80℃から150
℃まで昇温すれば足り(図4:T2 〜T3 )、この場合
も熱媒油加熱ボイラ13を小型化することができる。
As a result, the air in the furnace is heated by the heat insulation fan 17
Is sucked from the return duct 7 and heat-exchanged with the heat medium oil by the heat exchanger 8, and the heated air is fed into the furnace through the supply duct 9 and the temperature inside the furnace gradually rises. . Then, when the operation of the coating / drying apparatus 1 is restarted (8:30 am), the temperature inside the furnace reaches a preset temperature (for example, 80 ° C.), and here the heating oil heating boiler 13 and the hot air circulating fan 10 are used. When activated, the temperature rises from 80 ℃ to 150
It is sufficient to raise the temperature to ° C (Fig. 4: T 2 to T 3 ), and in this case as well, the heating oil heating boiler 13 can be downsized.

【0028】図4は本発明に係る他の塗装乾燥装置を示
すフローシート、図5はそのタイムチャートである。な
お、図1と共通する部分については同一符号を付して詳
細説明は省略する。本例では、塗装乾燥装置1の運転休
止時に保温ファン17を稼動させることに代えて、熱風
循環経路11に介装された熱風循環ファン10を例えば
インバータ制御して回転数を落とし小風量で稼動させる
ようにしている。
FIG. 4 is a flow sheet showing another coating drying apparatus according to the present invention, and FIG. 5 is a time chart thereof. In addition, the same reference numerals are given to portions common to FIG. 1 and detailed description is omitted. In this example, instead of operating the heat insulation fan 17 when the coating drying apparatus 1 is not operating, the hot air circulation fan 10 interposed in the hot air circulation path 11 is controlled by, for example, an inverter to reduce the rotation speed and operate with a small air volume. I am trying to let you.

【0029】すなわち、塗装乾燥装置1の運転が終了す
ると、開閉扉4,4が閉塞されると共に、大風量で運転
されていた熱風循環ファン10及び熱媒油加熱ボイラ1
3が停止され、炉内温度は徐々に低下する(図5:
0 )。そして、温度センサ20で検出された炉内温度
が予め設定された温度(例えば80℃)以下に下がる
と、通常の回転数よりも低い回転数で熱風循環ファン1
0を回転させる制御信号が制御装置19から出力され、
熱風循環経路11内に小風量で空気が循環される(図
5:T1 〜T2 )。このとき、熱交換器8には、発電装
置16の排熱により加熱された熱媒油が供給されている
ので、その熱により熱風循環経路11を循環する空気が
加熱され、これが炉内に送給されて炉内温度が上昇す
る。
That is, when the operation of the coating / drying apparatus 1 is completed, the opening / closing doors 4 and 4 are closed, and the hot air circulating fan 10 and the heat medium oil heating boiler 1 which have been operated with a large air volume.
3 is stopped and the temperature in the furnace gradually decreases (Fig. 5:
T 0 ). Then, when the temperature inside the furnace detected by the temperature sensor 20 falls below a preset temperature (for example, 80 ° C.), the hot air circulation fan 1 is rotated at a rotational speed lower than the normal rotational speed.
A control signal for rotating 0 is output from the control device 19,
A small amount of air is circulated in the hot air circulation path 11 (FIG. 5: T 1 to T 2 ). At this time, since the heat transfer oil heated by the exhaust heat of the power generator 16 is supplied to the heat exchanger 8, the heat circulates the air circulating in the hot air circulation path 11 and sends it to the furnace. It is supplied and the temperature in the furnace rises.

【0030】次いで、温度センサ20で検出された炉内
温度が予め設定された温度(例えば80℃)に達する
と、熱風循環ファン10の回転が停止され(図5:
2 )、これを繰り返しながら、炉内温度を約80℃の
保温温度に維持する。そして、塗装乾燥炉1の運転を再
開するときは、熱風循環ファン10を通常の回転数で運
転すると同時に、熱媒油加熱ボイラ13を起動させて、
各トンネル形炉3の炉内を所定の使用温度(例えば 150
℃) まで昇温する(図5:T3 〜T4)。この場合も、
80℃から150℃まで昇温すれば足り、熱媒油加熱ボ
イラ13を小型化することができる。なお、熱風循環フ
ァン10を小風量で運転する場合に、炉内温度を温度セ
ンサ20で検出する場合に限らず、タイマーを用いて塗
装乾燥装置1の運転再開時の一定時間前に運転開始する
ようにしてもよい。
Next, when the temperature inside the furnace detected by the temperature sensor 20 reaches a preset temperature (for example, 80 ° C.), the rotation of the hot air circulation fan 10 is stopped (FIG. 5:
T 2 ), while repeating this, the temperature in the furnace is maintained at a heat retention temperature of about 80 ° C. Then, when the operation of the coating drying furnace 1 is restarted, the hot air circulating fan 10 is operated at a normal rotation speed and, at the same time, the heating medium oil heating boiler 13 is activated,
The inside of each tunnel furnace 3 has a specified operating temperature (for example, 150
(° C.) (FIG. 5: T 3 to T 4 ). Also in this case,
It is sufficient to raise the temperature from 80 ° C. to 150 ° C., and the heating oil heating boiler 13 can be downsized. In addition, when the hot air circulation fan 10 is operated with a small air volume, the operation is not limited to the case where the temperature sensor 20 detects the temperature inside the furnace, and the operation is started before a fixed time when the operation of the coating drying apparatus 1 is restarted using a timer. You may do it.

【0031】[0031]

【発明の効果】以上述べたように、本発明によれば、塗
装乾燥装置の運転休止時に、非常用発電装置の排熱を利
用してトンネル形炉の炉内を保温しており、運転再開時
には保温されている炉内を使用温度まで昇温すれば足り
るので、同一時間内で昇温するのであれば、室温から使
用温度まで昇温する場合に比して熱量が少なくて済み、
したがって、熱媒油加熱ボイラを小型化して設備費を軽
減することができるという大変優れた効果を有する。
As described above, according to the present invention, when the operation of the coating dryer is stopped, the exhaust heat of the emergency power generator is used to keep the inside of the tunnel furnace warm, and the operation is restarted. Sometimes it is enough to raise the temperature of the inside of the furnace that is kept warm to the operating temperature, so if the temperature is raised within the same time, the amount of heat is less than when heating from room temperature to the operating temperature.
Therefore, there is a very excellent effect that the heating oil heating boiler can be downsized and the facility cost can be reduced.

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

【図1】本発明に係る塗装乾燥装置を示すフローシー
ト。
FIG. 1 is a flow sheet showing a coating / drying apparatus according to the present invention.

【図2】そのタイムチャート。FIG. 2 is its time chart.

【図3】他の実施例を示すタイムチャート。FIG. 3 is a time chart showing another embodiment.

【図4】本発明に係る他の塗装乾燥装置を示すフローシ
ート。
FIG. 4 is a flow sheet showing another coating drying apparatus according to the present invention.

【図5】そのタイムチャート。FIG. 5 is a time chart thereof.

【符号の説明】[Explanation of symbols]

1・・・塗装乾燥装置 2・・・出入口 3・・・トンネル形炉 4・・・開閉扉 7・・・リターンダクト 8・・・熱交換器 9・・・サプライダクト 10・・・熱風循環
ファン 11・・・熱風循環経路 12・・・熱媒油
循環配管 13・・・熱媒油加熱ボイラ 14・・・熱交換
器 15・・・燃焼室 16・・・発電装
置 17・・・保温ファン 18・・・バイパ
ス路 19・・・制御装置 20・・・温度セ
ンサ
1 ... Coating drying device 2 ... Doorway 3 ... Tunnel furnace 4 ... Opening door 7 ... Return duct 8 ... Heat exchanger 9 ... Supply duct 10 ... Hot air circulation Fan 11 ... Hot air circulation path 12 ... Heat oil oil circulation piping 13 ... Heat oil oil heating boiler 14 ... Heat exchanger 15 ... Combustion chamber 16 ... Power generator 17 ... Heat insulation Fan 18 ... Bypass 19 ... Control device 20 ... Temperature sensor

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 両端に出入口(2, 2)を開口したトンネ
ル形炉(3)に、その炉内からリターンダクト(7)を
通じて吸引した熱風を熱交換器(8)から供与される熱
で使用温度に加熱してサプライダクト(9)から再び炉
内に導入する熱風循環ファン(10)を介装した熱風循環
経路(11)が設けられた塗装乾燥装置において、前記熱
交換器(8)に、塗装設備の非常用電源となる電力を発
生する発電装置(16)の排熱によって加熱された熱媒油
を循環供給する熱媒油循環配管(12)が接続され、前記
トンネル形炉(3)の出入口(2, 2)には、その出入口
(2, 2)を塗装乾燥装置の運転休止時に閉塞する開閉扉
(4, 4) が設けられ、前記熱風循環経路(11)には、塗
装乾燥装置の運転休止時に前記熱交換器(8)が放出す
る熱で加熱された空気を前記トンネル形炉の炉内に送風
する保温ファン(17)を介装したバイパス路(18)が形
成されていることを特徴とする塗装乾燥装置。
1. A tunnel-type furnace (3) having openings (2, 2) at both ends, hot air sucked from inside the furnace through a return duct (7) is supplied with heat from a heat exchanger (8). The heat exchanger (8) in a coating drying apparatus provided with a hot air circulation path (11) having a hot air circulation fan (10) which is heated to a working temperature and introduced again into the furnace from a supply duct (9). Is connected to a heat medium oil circulation pipe (12) for circulating and supplying heat medium oil heated by exhaust heat of a power generation device (16) that generates electric power that serves as an emergency power source for coating equipment. The doorway (2, 2) of 3) is provided with an opening / closing door (4, 4) that closes the doorway (2, 2) when the coating dryer is not operating, and the hot air circulation path (11) is The air heated by the heat released by the heat exchanger (8) when the coating dryer is stopped is Paint drying apparatus characterized by bypass the heat insulating fan (17) is interposed for blowing air to the tunnel shape furnace in the furnace (18) is formed.
【請求項2】 前記トンネル形炉(3)の雰囲気温度が
所定の温度以下になった時に前記保温ファン(17)を稼
動する制御装置(19) を備えた請求項1記載の塗装乾燥
装置。
2. The coating / drying apparatus according to claim 1, further comprising a control device (19) for operating the heat insulation fan (17) when the atmospheric temperature of the tunnel furnace (3) becomes lower than a predetermined temperature.
【請求項3】 塗装乾燥装置の運転を再開する一定時間
前にタイマーから出力されるスイッチ信号によって前記
保温ファン(17)を稼動開始する制御装置(19)を備え
た請求項1記載の塗装乾燥装置。
3. The coating / drying apparatus according to claim 1, further comprising a control device (19) for starting the operation of the heat insulation fan (17) by a switch signal output from a timer at a predetermined time before restarting the operation of the coating / drying apparatus. apparatus.
【請求項4】 両端に出入口(2, 2)を開口したトンネ
ル形炉(3)に、その炉内からリターンダクト(7)を
通じて吸引した熱風を熱交換器(8)から供与される熱
で使用温度に加熱してサプライダクト(9)から再び炉
内に導入する熱風循環ファン(10)を介装した熱風循環
経路(11)が設けられた塗装乾燥装置において、前記熱
交換器(8)に、塗装設備の非常用電源となる電力を発
生する発電装置(16)の排熱によって加熱された熱媒油
を循環供給する熱媒油循環配管(12)が接続され、前記
トンネル形炉(3)の出入口(2, 2)には、その出入口
(2, 2)を塗装乾燥装置の運転休止時に閉塞する開閉扉
(4, 4)が設けられ、塗装乾燥装置の運転休止時に前記
熱交換器(8)が放出する熱で加熱された空気を前記ト
ンネル形炉(3)の炉内に送風し得る程度の小風量で前
記熱風循環ファン(10)を稼動させる制御装置(19)を
備えたことを特徴とする塗装乾燥装置。
4. A tunnel type furnace (3) having openings (2, 2) at both ends is provided with hot air sucked from inside the furnace through a return duct (7) by heat supplied from a heat exchanger (8). The heat exchanger (8) in a coating drying apparatus provided with a hot air circulation path (11) having a hot air circulation fan (10) which is heated to a working temperature and introduced again into the furnace from a supply duct (9). Is connected to a heat medium oil circulation pipe (12) for circulating and supplying heat medium oil heated by exhaust heat of a power generation device (16) that generates electric power that serves as an emergency power source for coating equipment. The doorway (2, 2) of 3) is provided with an opening / closing door (4, 4) that closes the doorway (2, 2) when the coating drying apparatus is not operating, and the heat exchange is performed when the coating drying apparatus is not operating. The air heated by the heat emitted from the vessel (8) is sent into the furnace of the tunnel furnace (3). A coating drying apparatus comprising a control device (19) for operating the hot air circulation fan (10) with a small air volume that can be blown.
JP14752394A 1994-06-29 1994-06-29 Coating drying device Pending JPH0810679A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14752394A JPH0810679A (en) 1994-06-29 1994-06-29 Coating drying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14752394A JPH0810679A (en) 1994-06-29 1994-06-29 Coating drying device

Publications (1)

Publication Number Publication Date
JPH0810679A true JPH0810679A (en) 1996-01-16

Family

ID=15432248

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14752394A Pending JPH0810679A (en) 1994-06-29 1994-06-29 Coating drying device

Country Status (1)

Country Link
JP (1) JPH0810679A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101034006B1 (en) * 2010-07-20 2011-05-11 리턴에너지 주식회사 Dryer for removing plume and environment pollution and for recovering energy
KR101242649B1 (en) * 2010-03-11 2013-03-19 주식회사 쎄코 Dryer system of leather automatic painting apparatus
JP2018112366A (en) * 2017-01-13 2018-07-19 パーカーエンジニアリング株式会社 Coating line

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101242649B1 (en) * 2010-03-11 2013-03-19 주식회사 쎄코 Dryer system of leather automatic painting apparatus
KR101034006B1 (en) * 2010-07-20 2011-05-11 리턴에너지 주식회사 Dryer for removing plume and environment pollution and for recovering energy
JP2018112366A (en) * 2017-01-13 2018-07-19 パーカーエンジニアリング株式会社 Coating line

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