JPH0335989B2 - - Google Patents
Info
- Publication number
- JPH0335989B2 JPH0335989B2 JP21167081A JP21167081A JPH0335989B2 JP H0335989 B2 JPH0335989 B2 JP H0335989B2 JP 21167081 A JP21167081 A JP 21167081A JP 21167081 A JP21167081 A JP 21167081A JP H0335989 B2 JPH0335989 B2 JP H0335989B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- furnace
- gas
- heat treatment
- treatment furnace
- 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
- 239000007789 gas Substances 0.000 claims description 100
- 238000010438 heat treatment Methods 0.000 claims description 50
- 238000002156 mixing Methods 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 18
- 230000008859 change Effects 0.000 claims description 2
- 229910000831 Steel Inorganic materials 0.000 description 16
- 239000010959 steel Substances 0.000 description 16
- 239000003973 paint Substances 0.000 description 15
- 230000004043 responsiveness Effects 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000523 sample Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000001877 deodorizing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000004913 activation Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 238000007602 hot air drying Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
- C21D1/767—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material with forced gas circulation; Reheating thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Drying Of Solid Materials (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Coating Apparatus (AREA)
- Control Of Heat Treatment Processes (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、熱風循環式熱処理炉の温度制御方
法及び装置に関するものであつて、一層詳細には
炉内で熱風を循環させて物品の熱処理を行う熱処
理炉の炉内温度を極めて応答性良く制御し得ると
共に、炉中に挿入される物品の熱負荷に変動が生
じても熱エネルギーの廃棄を抑制して省エネルギ
ーを達成し得るようにした炉内温度制御方法及び
その装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a temperature control method and apparatus for a hot air circulation type heat treatment furnace, and more particularly, it relates to a temperature control method and apparatus for a hot air circulation type heat treatment furnace, and more specifically, for heat treating articles by circulating hot air in the furnace. Furnace temperature in a heat treatment furnace can be controlled with extremely high responsiveness, and even if the heat load of articles inserted into the furnace fluctuates, waste of thermal energy can be suppressed to achieve energy savings. The present invention relates to a temperature control method and device.
従来技術
限定空間内に高温気体を供給し、この高温気体
をフアンにより熱風として該空間内に循環させて
物品の各種熱処理を行う所謂熱風循環式熱処理炉
が、産業界において好適に使用されている。この
種の熱風循環式熱処理炉としては、カラー塗装鋼
板の塗料乾燥焼付炉やプラスチツクフイルムの製
造工程で使用される熱風吹付による加熱炉等があ
り、加熱源としての高温気体は、溶鉱炉、燃焼炉
その他燃焼脱臭装置から副次生産される各種燃焼
排ガスや加熱空気が一般に使用される。この場
合、炉中で熱処理される被処理対象物の熱容量そ
の他の性状に応じて、炉内に供給される高温気体
の温度が最適値になるよう温度制御をする必要が
あるが、炉内温度に極めて微妙な制御が要求され
るような場合、これに忠実に応答して追従制御す
ることは一般に困難であつた。PRIOR ART A so-called hot air circulation heat treatment furnace, which supplies high-temperature gas into a limited space and circulates the high-temperature gas as hot air within the space using a fan to perform various heat treatments on articles, is suitably used in industry. . Examples of this type of hot air circulation heat treatment furnace include paint drying and baking furnaces for color-coated steel plates and heating furnaces that blow hot air used in the manufacturing process of plastic films. Other types of combustion exhaust gas and heated air produced as by-products from combustion deodorizing equipment are generally used. In this case, it is necessary to control the temperature of the high-temperature gas supplied into the furnace to an optimal value depending on the heat capacity and other properties of the object to be heat-treated in the furnace. In cases where extremely delicate control is required, it has generally been difficult to faithfully respond and perform follow-up control.
そこで出願人は、前記熱風循環式熱処理炉に好
適に使用されて応答性の良好な温度制御を達成し
得る「温度調節装置」を開発し、これについて先
に特許出願を行つた。これは、第1図に示すよう
に熱風循環式熱処理炉10に連通接続する高温気
体供給管12の管路中に隔壁14を長手方向に延
設してバイパス管路16及び熱交換管路18を
夫々画成し、前記熱交換管路18に熱交換器20
を内設し、更に両管路の連通開口部に開閉蓋22
(例えば、フラツプ状のダンパ)を両管路の開口
比率を調節し得るように配設したことを概略的な
要旨としている。この場合、高温気体は燃焼加熱
装置24で高温加熱された後、高温気体供給管1
2を介して前記バイパス管路16及び熱交換管路
18に供給され、このとき前記開閉蓋22の開度
によつて各管路16,18への高温気体の供給割
合が振り分けられ、熱交換器20と接触して温度
降下した気体とバイパス管路16を通過して温度
降下のしていない気体とが両管路の連通出口で混
合されて、所定温度に調節制御される。なお、開
閉蓋22の開度調節は、熱処理炉10に挿入した
温度検出器26により検出した炉内温度に応じて
自動的になされる。この温度調節装置によれば、
応答性が良好でかつ精度の高い炉内温度制御がな
されるが、前記熱交換管路18において高温気体
の熱エネルギーの一部は熱交換器20により奪取
され、排棄されるので、省エネルギーの見地から
は経済効率が劣る欠点がある。すなわち、熱処理
炉10中に挿入される被処理物品は、その材質や
外形寸法等に応じて熱負荷が異るものであるか
ら、異る寸法の物品を挿入したときはその熱負荷
の変動に応じて炉内温度を調節する必要が生ずる
訳であるが、前記温度制御装置ではこの熱負荷の
変動に応じて高温気体の供給量を制御することは
できないため、熱負荷の小さい物品に対応して温
度制御するときは高温気体から相当多量の熱エネ
ルギーを熱交換器20により奪取する必要があ
り、エネルギー損失が大きかつた訳である。 Therefore, the applicant has developed a "temperature control device" that can be suitably used in the hot air circulation type heat treatment furnace to achieve temperature control with good responsiveness, and has previously filed a patent application for this. As shown in FIG. 1, a partition wall 14 is longitudinally extended in the high temperature gas supply pipe 12 which is connected to the hot air circulation type heat treatment furnace 10 to form a bypass pipe 16 and a heat exchange pipe 18. and a heat exchanger 20 in the heat exchange pipe 18.
is installed internally, and an opening/closing lid 22 is provided at the communication opening of both pipes.
The general gist is that a damper (for example, a flap-shaped damper) is arranged so that the opening ratio of both pipes can be adjusted. In this case, the high-temperature gas is heated to a high temperature by the combustion heating device 24, and then the high-temperature gas supply pipe 1
2 to the bypass pipe line 16 and the heat exchange pipe line 18, and at this time, the proportion of high temperature gas supplied to each pipe line 16, 18 is distributed depending on the degree of opening of the opening/closing lid 22, and the heat exchange The gas whose temperature has dropped by contacting the vessel 20 and the gas whose temperature has not dropped after passing through the bypass pipe 16 are mixed at the communicating outlet of both pipes, and the temperature is adjusted to a predetermined temperature. Note that the opening degree of the opening/closing lid 22 is automatically adjusted according to the temperature inside the furnace detected by a temperature detector 26 inserted into the heat treatment furnace 10. According to this temperature control device,
Although the temperature inside the furnace is controlled with good responsiveness and high precision, a part of the thermal energy of the high-temperature gas in the heat exchange pipe 18 is taken by the heat exchanger 20 and discarded. From a viewpoint, it has the disadvantage of being less economically efficient. In other words, the heat load of the articles inserted into the heat treatment furnace 10 varies depending on their material, external dimensions, etc., so when articles of different sizes are inserted, the heat load changes. Therefore, it is necessary to adjust the temperature inside the furnace accordingly, but since the temperature control device cannot control the supply amount of high temperature gas according to the fluctuations in the heat load, When controlling the temperature using the heat exchanger 20, it is necessary to extract a considerable amount of thermal energy from the high-temperature gas using the heat exchanger 20, resulting in a large energy loss.
そこで、熱エネルギーを僅かでも逃出させるこ
とく炉内温度の調節を図ろうとするならば、第2
図にモデル化したような熱ループが考えられる。
すなわち、熱処理炉10と高温気体供給管12と
により熱循環系を構成し、前記高温気体供給管1
2に流量制御弁28を介挿するものである。この
とき、熱処理炉10は、内部容積が一定に限定さ
れた密閉空間と考えてよいから、高温気体供給管
12により炉中に供給される高温気体の流量を前
記流量制御弁28により調節してやれば、一定の
制限空間に供給される高温気体の流量の増減によ
り包蔵熱エネルギー量も増減するので、炉内温度
の調節をなし得ることになる。 Therefore, if you want to adjust the temperature inside the furnace without allowing even a small amount of thermal energy to escape, the second
A thermal loop like the one modeled in the figure can be considered.
That is, the heat treatment furnace 10 and the high temperature gas supply pipe 12 constitute a thermal circulation system, and the high temperature gas supply pipe 1
2, a flow control valve 28 is inserted therein. At this time, since the heat treatment furnace 10 can be considered to be a closed space with a fixed internal volume, the flow rate of the high temperature gas supplied into the furnace through the high temperature gas supply pipe 12 may be adjusted by the flow rate control valve 28. As the amount of stored thermal energy increases or decreases as the flow rate of high-temperature gas supplied to a certain restricted space increases or decreases, the temperature inside the furnace can be adjusted.
発明が解決すべき課題
しかるにこの構成では、高温気体のもつ熱エネ
ルギーは前記熱ループを循環するだけで熱交換器
等により積極的に奪取されることはないから、エ
ネルギーの有効利用の見地からは優れているが、
熱負荷の変動に対する応答性が不良で極めて大ま
かな温度調節しかできないため、被処理対象物の
厳しい温度要求に応じて微妙に炉内の温度調節を
する必要のある産業用の熱処理炉には採用し得な
かつた。Problems to be Solved by the Invention However, in this configuration, the thermal energy of the high-temperature gas only circulates through the heat loop and is not actively captured by a heat exchanger, etc., so from the standpoint of effective energy use, Excellent, but
Because it has poor responsiveness to changes in heat load and can only make very rough temperature adjustments, it is used in industrial heat treatment furnaces that require delicate temperature adjustment in response to the strict temperature requirements of the objects to be treated. I couldn't do it.
発明の目的
本発明は、このような現状に鑑みて案出された
ものであつて、炉内温度に対する応答性に優れ精
度の良い制御を可能にすると共に、炉中に挿入さ
れる物品の熱負荷の変動に応じて高温気体からの
熱エネルギーの奪取を必要最小限に抑制し、操業
効率を高めることを目的とする。Purpose of the Invention The present invention has been devised in view of the current situation, and enables highly responsive and accurate control of the temperature inside the furnace, as well as controlling the heat of articles inserted into the furnace. The purpose is to increase operational efficiency by suppressing the extraction of thermal energy from high-temperature gas to the necessary minimum in response to load fluctuations.
課題を解決するための手段
この目的を達成するため本発明に係る熱風循環
式熱処理炉の温度制御方法は、高温気体と該高温
気体の一部を熱交換して温度差を生じさせた気体
とを気体混合手段を介して熱風循環式熱処理炉に
供給するに際し、前記温度差のある両気体の混合
比が一定になるよう前記気体混合手段の混合比調
節手段を制御した後、前記気体混合手段に供給さ
れる高温気体の流量を制御し、前記熱風循環式熱
処理炉の炉内温度が安定した後、その炉内温度を
検出して前記気体混合手段の混合比調節手段を制
御して、前記温度差のある両気体の混合比を変化
させることを特徴とする。Means for Solving the Problems In order to achieve this object, the temperature control method for a hot air circulation heat treatment furnace according to the present invention provides a method for controlling the temperature of a hot air circulation heat treatment furnace, in which a high temperature gas and a part of the high temperature gas are heat exchanged to generate a temperature difference. When supplying the gas to the hot air circulation type heat treatment furnace through the gas mixing means, after controlling the mixing ratio adjusting means of the gas mixing means so that the mixing ratio of the two gases having the temperature difference becomes constant, the gas mixing means After the temperature inside the hot air circulation heat treatment furnace is stabilized, the temperature inside the furnace is detected and the mixing ratio adjusting means of the gas mixing means is controlled. It is characterized by changing the mixing ratio of both gases with a temperature difference.
また、この温度制御方法を好適に実施するため
に使用される温度制御装置は、熱風循環式熱処理
炉に高温気体供給管を接続し、この高温気体供給
管の管路の一部をバイパス管路と熱交換管路とに
画成し、前記両管路における高温気体入口側の連
通開口部に各管路の開口比率を調節可能な開閉蓋
を設け、前記両管路の高温気体入口側と連通する
前記高温気体供給管に流量制御弁を介挿し、更に
前記熱処理炉に炉内温度検出器を配設して、これ
による検出温度に応じて前間開閉蓋または流量制
御弁の開度を選択的に制御するよう構成すること
を特徴とする。 In addition, the temperature control device used to suitably implement this temperature control method connects a high-temperature gas supply pipe to a hot air circulation type heat treatment furnace, and connects a part of the high-temperature gas supply pipe to a bypass pipe. and a heat exchange pipe, and an opening/closing lid that can adjust the opening ratio of each pipe is provided at the communication opening on the high temperature gas inlet side of both the pipes, and the high temperature gas inlet side of both the pipes A flow rate control valve is inserted into the communicating high-temperature gas supply pipe, and an in-furnace temperature detector is further provided in the heat treatment furnace, and the opening degree of the front opening/closing lid or the flow rate control valve is controlled according to the detected temperature. It is characterized by being configured to selectively control.
実施例
次に、本発明に係る温度制御方法及び装置につ
き、実施例を挙げて、添付図面を参照しながら以
下詳細に説明する。Embodiments Next, the temperature control method and apparatus according to the present invention will be described in detail by way of embodiments with reference to the accompanying drawings.
第3図は本発明に係る熱風循環式熱処理炉の温
度制御方法を好適に実施し得る熱風循環式熱処理
炉の温度制御装置の概略構成を示すものであつ
て、参照符号30は耐熱性材料で囲われて略密閉
空間を形成する熱処理炉を示す。前記熱処理炉3
0の外方に気体加熱装置32を配設し、この気体
加熱装置32の出口部から高温気体供給管34を
導出して、その先端を熱処理炉30に連通接続す
る。また熱処理炉30から気体吸引管36を導出
し、吸引送風機38を介して前記気体加熱装置3
2の入口部に接続する。これによつて熱処理炉3
0に対する高温気体循環系が構成される。 FIG. 3 shows a schematic configuration of a temperature control device for a hot air circulation type heat treatment furnace that can suitably implement the temperature control method for a hot air circulation type heat treatment furnace according to the present invention, and reference numeral 30 is a heat-resistant material. A heat treatment furnace is shown that is surrounded to form a substantially closed space. The heat treatment furnace 3
A gas heating device 32 is disposed outside of the gas heating device 32, and a high temperature gas supply pipe 34 is led out from the outlet of the gas heating device 32, and its tip is connected to the heat treatment furnace 30 in communication. Further, a gas suction pipe 36 is led out from the heat treatment furnace 30, and the gas heating device 3 is passed through a suction blower 38.
Connect to the inlet of No.2. As a result, the heat treatment furnace 3
A high temperature gas circulation system for 0 is constructed.
熱処理炉30側に接続している前記高温気体供
給管34の管路の一部を第3図に示すように膨隆
させ、その膨隆部内部に管路長手方向に沿つて隔
壁40を延設して、熱交換負荷の設けられていな
いバイパス管路42と、熱交換器44を内設した
熱交換管路46とに画成する。このバイパス管路
42及び熱交換管路46の各開口部が連通し合う
個所(殊に好ましくは、高温気体の入口側におけ
る連通個所)に、一端部を軸支されてフラツプ動
作をし前記各管路の開口比率を調節可能なダンパ
状の開閉蓋48を配設し、前記バイパス管路42
及び熱交換管路46を含む全体として後述する温
度差のある両気体の混合手段を構成する。なお、
前記開閉蓋48は作動杆50を介して適宜のアク
チユエータ52に接続する。このアクチユエータ
52としては、電動モータ駆動のリニアアクチユ
エータが好適に使用される。また前記熱処理炉3
0に、好ましくは熱電対からなる温度検出器54
を配設してその測温プローブ56を炉中の所望温
度検出域に臨ませ、この温度検出器54による検
出値を温度制御回路58に入力するように構成す
る。温度制御回路58はその演算検出温度に応じ
て適宜の指令を前記アクチユエータ52に送り、
これによつて開閉蓋48の開度を調節するように
なつている。 A part of the high-temperature gas supply pipe 34 connected to the heat treatment furnace 30 side is swollen as shown in FIG. 3, and a partition wall 40 is provided extending inside the swollen portion along the longitudinal direction of the pipe. A bypass pipe 42 with no heat exchange load and a heat exchange pipe 46 with a heat exchanger 44 installed therein are defined. One end of the bypass pipe 42 and the heat exchange pipe 46 is pivotally supported at a location where the openings communicate with each other (particularly preferably, a communication location on the high temperature gas inlet side) for flap operation. A damper-like opening/closing lid 48 that can adjust the opening ratio of the pipeline is provided, and the bypass pipeline 42 is
and the heat exchange pipe 46 as a whole constitute means for mixing both gases having a temperature difference, which will be described later. In addition,
The opening/closing lid 48 is connected to a suitable actuator 52 via an operating rod 50. As this actuator 52, an electric motor-driven linear actuator is preferably used. Further, the heat treatment furnace 3
0, a temperature sensor 54, preferably consisting of a thermocouple.
is arranged so that its temperature measuring probe 56 faces a desired temperature detection area in the furnace, and the detected value by this temperature detector 54 is input to a temperature control circuit 58. The temperature control circuit 58 sends an appropriate command to the actuator 52 according to the calculated detected temperature,
This allows the degree of opening of the opening/closing lid 48 to be adjusted.
また、前記バイパス管路42及び熱交換管路4
6の高温気体入口側に連通する高温気体供給管3
4に流量制御弁60を介挿し、この流量制御弁6
0を駆動する例えば電動トルクモータからなるア
クチユエータ62を設けて、先と同様に温度検出
器54に接続する温度制御回路64から、このア
クチユエータ62の付勢指令を送り、流量制御弁
60の弁開度を調節する。なお、2つのアクチユ
エータ52,62は、温度検出器54から共通の
温度情報を受けるが、例えば流量制御弁60の弁
開度調節が終了してから開閉蓋48の開度調節が
なされるように、予め設定したシーケンスプログ
ラムに従つて選択的に作動するようになつてい
る。 In addition, the bypass pipe line 42 and the heat exchange pipe line 4
High temperature gas supply pipe 3 communicating with the high temperature gas inlet side of 6
A flow control valve 60 is inserted into 4, and this flow control valve 6
An actuator 62 made of, for example, an electric torque motor is provided to drive the flow rate control valve 60, and a temperature control circuit 64 connected to the temperature sensor 54 sends an activation command to the actuator 62 to open the flow rate control valve 60. Adjust the degree. Note that the two actuators 52 and 62 receive common temperature information from the temperature detector 54, but for example, the opening degree of the opening/closing lid 48 is adjusted after the valve opening degree adjustment of the flow rate control valve 60 is completed. , is adapted to operate selectively according to a preset sequence program.
本発明に係る温度制御方法を実施するには、次
のように前記温度制御装置を操作する。バイパス
管路42及び熱交換管路46の開口比率を変化さ
せる開閉蓋48の開度を適宜制御し(例えば熱交
換管路46における開度を30%に設定)、高温気
体と該高温気体の一部を熱交換して降温させ温度
差を生じさせた気体との混合比が一定となるよう
予じめ設定しておいてから、流量制御弁60の弁
開度調節により前記気体混合手段に供給される高
温気体の流量を加減し、これによつて炉中温度の
大まかな設定を行う。次いで炉中温度が安定して
から開閉蓋48の開度調節をし、所望温度への厳
密な調節を行うことによつて、応答性に優れ精度
の高い温度制御を達成することができる。本発明
に係る温度制御方法及び装置は、カラー塗装鋼板
製造用の塗料焼付炉に使用すると極めて有効であ
るので、本発明の作用効果の詳細について、この
塗料焼付炉に使用した場合の実施例との関連で以
下説明する。 To carry out the temperature control method according to the present invention, the temperature control device is operated as follows. The degree of opening of the opening/closing lid 48 that changes the opening ratio of the bypass line 42 and the heat exchange line 46 is appropriately controlled (for example, the degree of opening of the heat exchange line 46 is set to 30%), and the high temperature gas and the high temperature gas are After setting in advance so that the mixing ratio with the gas whose temperature is lowered through heat exchange to cause a temperature difference is constant, the gas mixing means is adjusted by adjusting the valve opening of the flow rate control valve 60. The flow rate of the high-temperature gas supplied is adjusted, thereby roughly setting the temperature inside the furnace. Next, after the temperature in the furnace has stabilized, the opening degree of the opening/closing lid 48 is adjusted to precisely adjust the temperature to a desired temperature, thereby achieving highly responsive and highly accurate temperature control. The temperature control method and device according to the present invention are extremely effective when used in a paint baking furnace for producing color-coated steel sheets. This will be explained below in connection with this.
第4図は、本発明に係る温度制御方法及び装置
が好適に使用されるカラー塗装鋼板製造用の塗料
焼付炉の概略構造を示し、併せて先に説明した第
3図にこの塗料焼付炉の内部横断面を示す。第4
図において参照符号30は、熱風循環式熱処理炉
としての塗料焼付炉を示し、この炉中に所定間隔
を保持して対向配置したプレナムチヤンバ66,
68の間に塗料塗布したカラー鋼板70が通さ
れ、各プレナムチヤンバの対向面に開設したノズ
ル72から噴出する熱風によつて前記カラー鋼板
70は無接触で浮遊走行するようになつている。
すなわち、第3図から判明するように各プレナム
チヤンバ66,68はダクト74,76を介して
送風機78の送風口に連通接続し、またこの送風
機78は吸気口80を介して炉中の高温気体を吸
引加圧し、前記ノズル72から熱風をカラー鋼板
70に向けて上下に噴射して、動圧及び静圧のバ
ランスを図ることによつてカラー鋼板70を浮遊
させるものである。塗料焼付炉30は第4図に示
すように蒸発帯Aと硬化帯Bとに別たれ、またプ
レナムチヤンバ66,68は図示のように複数の
区分に画成され、夫々の区分に対応するように前
記高温気体供給管34が炉30に接続開口してい
る。この高温気体供給管34に、第3図に示す本
発明に係る温度制御装置が夫々配設される。そし
て、鋼板70は下地処理が行われた後、コータ8
2によりカラー塗料を塗布され、炉中を浮遊走行
する際に前記蒸発帯Aで溶剤を蒸発させ、次いで
硬化帯Bで硬化させて塗膜の焼付を行う。なお、
第4図において参照符号84は強制空冷室、86
は水冷室、88は熱風乾燥装置を夫々示し、カラ
ー鋼板70は必要に応じて2〜3回同じ工程を通
されて重ね塗りがなされる(本実施例では2回)。 FIG. 4 shows a schematic structure of a paint baking furnace for manufacturing color coated steel sheets in which the temperature control method and device according to the present invention are suitably used. Internal cross section shown. Fourth
In the figure, reference numeral 30 indicates a paint baking furnace as a hot air circulation heat treatment furnace, and plenum chambers 66, 66 and
A colored steel plate 70 coated with paint is passed between the plenum chambers 68, and the colored steel plate 70 is caused to float without contact by hot air blown out from nozzles 72 provided on the opposing faces of each plenum chamber.
That is, as can be seen from FIG. 3, each plenum chamber 66, 68 is connected via ducts 74, 76 to an air outlet of a blower 78, and this blower 78 also carries hot gas in the furnace through an inlet 80. The color steel plate 70 is made to float by applying suction and pressurization and jetting hot air upward and downward toward the color steel plate 70 from the nozzle 72 to balance dynamic pressure and static pressure. The paint baking furnace 30 is divided into an evaporation zone A and a curing zone B, as shown in FIG. The high temperature gas supply pipe 34 has a connection opening to the furnace 30. A temperature control device according to the present invention shown in FIG. 3 is installed in each of the high temperature gas supply pipes 34. After the steel plate 70 is subjected to surface treatment, the coater 8
2, the color paint is applied, and as it floats through the oven, the solvent is evaporated in the evaporation zone A, and then it is cured in the curing zone B to bake the paint film. In addition,
In FIG. 4, reference numeral 84 is a forced air cooling chamber, and 86
Reference numeral 88 indicates a water cooling chamber, and 88 indicates a hot air drying device, and the color steel plate 70 is subjected to the same process two to three times as necessary to perform overcoating (two times in this embodiment).
炉中の蒸発溶剤を含有する気体は、吸引送風機
38により吸引され、吸引管36を介して脱臭加
熱装置32に送られ、バーナ90により蒸発溶剤
は自然温度にまで昇温されて燃焼脱臭される。同
時に気体は再加熱され、高温気体供給管34を経
て塗料焼付炉30に帰還する。 The gas containing the evaporated solvent in the furnace is sucked by the suction blower 38 and sent to the deodorizing heating device 32 via the suction pipe 36, and the evaporated solvent is heated to natural temperature by the burner 90 and deodorized by combustion. . At the same time, the gas is reheated and returned to the paint baking furnace 30 via the high temperature gas supply pipe 34.
このようなカラー鋼板製造用の塗料焼付炉にお
いて、本発明に係る温度制御装置は次のように操
作すると好適である。すなわち、例えば一旦休止
した炉の運転を再開するに際して、炉内温度を最
適値にまで昇温するには、熱負荷としてカラー鋼
板70を炉中に挿入した状態とし、熱交換管路4
6の開口部において前記開閉蓋48の開度を制御
して、例えば開度30%に設定しておく。これによ
つてバイパス管路42を通過する高温気体と、熱
交換管路46を通過し降温して温度差の生じた気
体との混合比が一定となるようにしておき、次い
で流量制御弁60を開放して、バイパス管路42
及び熱交換管路46からなる前記気体混合手段に
高温気体を供給し、温度差のある両気体の混合を
前記塗料焼付炉30中に送り込む。プレナムチヤ
ンバ68に挿入した熱電対54の測温プローブ5
6により炉内温度を検出して、温度制御回路64
によりアクチユエータ62を付勢し、前記流量制
御弁60の弁開度を調節して略所望の炉内温度を
得る。次いで別の温度制御回路58を作動させて
もう一方のアクチユエータ52を付勢し、開閉蓋
48の開度を調節する。これによつてバイパス管
路42と熱交換管路46との高温気体出口側にお
ける開口連通部における前記温度差のある両気体
の混合比が変化し、所望の温度に精度良く制御さ
れた高温気体が得られ、これを炉中に送り込むこ
とによつて炉内温度は熱負荷に応じて応答性良く
制御される。 In such a paint baking furnace for producing colored steel sheets, the temperature control device according to the present invention is preferably operated as follows. That is, for example, when restarting the operation of a furnace that has been temporarily suspended, in order to raise the temperature inside the furnace to the optimum value, the color steel plate 70 is inserted into the furnace as a heat load, and the heat exchange pipe 4 is
The opening degree of the opening/closing lid 48 at the opening 6 is controlled and set to, for example, 30%. As a result, the mixing ratio between the high-temperature gas passing through the bypass pipe 42 and the gas passing through the heat exchange pipe 46 and having a lower temperature resulting in a temperature difference is kept constant, and then the flow control valve 60 By opening the bypass pipe 42
A high temperature gas is supplied to the gas mixing means consisting of a heat exchange pipe 46 and a heat exchange pipe 46, and a mixture of both gases having a temperature difference is sent into the paint baking furnace 30. Temperature probe 5 of thermocouple 54 inserted into plenum chamber 68
6 detects the temperature inside the furnace and controls the temperature control circuit 64.
energizes the actuator 62 and adjusts the valve opening degree of the flow rate control valve 60 to obtain a substantially desired furnace temperature. Next, another temperature control circuit 58 is operated to energize the other actuator 52 and adjust the degree of opening of the opening/closing lid 48. As a result, the mixing ratio of the two gases having the temperature difference in the open communication section on the high temperature gas outlet side between the bypass pipe line 42 and the heat exchange pipe line 46 changes, and the high temperature gas is precisely controlled to a desired temperature. By feeding this into the furnace, the temperature inside the furnace can be controlled with good responsiveness according to the heat load.
なお、前記流量制御弁60により塗料焼付炉3
0に供給される高温気体の流量を変化させても、
この炉中への高温気体の供給流量とは独立して送
風機78がプレナムチヤンバ66,68から熱風
を鋼板70に吹付けるように構成されているか
ら、鋼板70の浮遊(フローテイング)走行には
全く支障は生じない。 Note that the flow rate control valve 60 controls the paint baking furnace 3.
Even if you change the flow rate of high temperature gas supplied to 0,
Since the blower 78 is configured to blow hot air from the plenum chambers 66 and 68 onto the steel plate 70 independently of the flow rate of high-temperature gas supplied into the furnace, there is no problem with the floating movement of the steel plate 70. No problems will occur.
このように、本発明に係る温度制御方法によれ
ば、温度差のある気体を相互に混合して熱風循環
式熱処理炉に供給するに際し、前記温度差のある
両気体の混合比が一定となるよう設定した後この
気体混合手段に供給される高温気体の流量を制御
し、かくして炉内温度が安定した後前記温度差の
ある両気体の混合比を変化させることにより、応
答性の良い炉内温度制御を達成し得るものであ
る。また、この温度制御方法を実施するための温
度制御装置として、熱風循環式熱処理炉に接続す
る高温気体供給管の管路系に、バイパス管路と熱
交換管路と開閉蓋とからなる温度差のある気体の
混合部と、流量制御弁とを備え、炉内温度に応じ
て選択的に順次作動させるよう構成することによ
り、被処理物品の熱容量その他の要因により決定
される炉中の要求温度に迅速に対応することがで
きる。 As described above, according to the temperature control method of the present invention, when gases having different temperatures are mixed and supplied to the hot air circulation heat treatment furnace, the mixing ratio of the two gases having different temperatures becomes constant. After the setting is made, the flow rate of high-temperature gas supplied to the gas mixing means is controlled, and after the temperature inside the furnace is stabilized, the mixing ratio of both gases with the temperature difference is changed, so that the inside of the furnace has good responsiveness. Temperature control can be achieved. In addition, as a temperature control device for implementing this temperature control method, a temperature difference between a bypass pipe, a heat exchange pipe, and an opening/closing lid is installed in the pipe system of the high-temperature gas supply pipe connected to the hot air circulation heat treatment furnace. The required temperature in the furnace determined by the heat capacity of the article to be processed and other factors can be adjusted by having a gas mixing section and a flow rate control valve, which are configured to operate selectively and sequentially depending on the temperature in the furnace. be able to respond quickly.
なお、本発明に係る温度制御装置でも、熱交換
管路46中に熱交換器44を備えているので、高
温気体がこれに接触する際に熱エネルギーは一部
奪取される訳であるが、本発明ではその前段に流
量制御弁60を配設したことにより、炉中の熱負
荷に変動が生じた場合その熱負荷に見合つた流量
だけの高温気体を熱交換管路46に分配供給すれ
ばよいので、熱交換により奪取される熱エネルギ
ー量を抑制し、省エネルギーに貢献し得るもので
ある。すなわち、第1図に示す構造の装置では、
炉中に挿入される熱負荷が例えば100から50に変
動した場合であつても、熱交換管路18を備える
気体混合部には常に一定の流量の高温気体が供給
されるため熱交換管路18において多量の熱交換
をする必要があり、熱損失が大きい。これに対し
第3図に示す本発明に係る装置では、炉中に挿入
される熱負荷が100から50に変動した場合は、こ
の熱負荷に見合つた流量の高温気体を気体混合部
に供給し得るため、熱交換により奪取される熱エ
ネルギーを必要最小限に抑制し得る。 In addition, since the temperature control device according to the present invention also includes the heat exchanger 44 in the heat exchange pipe 46, some of the thermal energy is taken away when the high temperature gas comes into contact with it. In the present invention, by disposing the flow rate control valve 60 at the front stage, when the heat load in the furnace fluctuates, high-temperature gas can be distributed and supplied to the heat exchange pipe 46 at a flow rate commensurate with the heat load. Therefore, the amount of thermal energy taken by heat exchange can be suppressed, contributing to energy saving. That is, in the device having the structure shown in FIG.
Even if the heat load inserted into the furnace changes from, for example, 100 to 50, a constant flow rate of high-temperature gas is always supplied to the gas mixing section equipped with the heat exchange pipe 18. 18, it is necessary to exchange a large amount of heat, resulting in large heat loss. On the other hand, in the device according to the present invention shown in Fig. 3, when the heat load inserted into the furnace changes from 100 to 50, high-temperature gas is supplied to the gas mixing section at a flow rate commensurate with this heat load. In order to achieve this, the thermal energy taken by heat exchange can be suppressed to the necessary minimum.
以上、本発明に係る熱風循環式熱処理炉の温度
制御方法及び装置について、カラー鋼板製造用の
塗料焼付炉に使用した場合を例に挙げて詳細に説
明したが、本発明はこの実施例に限定されるもの
ではなく、発明の精神の範囲内で種々改良、変更
をなし得るものである。 Above, the temperature control method and device for a hot air circulation heat treatment furnace according to the present invention have been explained in detail by taking as an example the case where it is used in a paint baking furnace for producing colored steel sheets, but the present invention is limited to this embodiment. However, various improvements and changes can be made within the spirit of the invention.
第1図及び第2図は従来技術に係る温度制御装
置の概略構成図、第3図は本発明に係る温度制御
方法を好適に実施し得る温度制御装置の概略構成
図であつて、第4図に示す実施例における炉の横
断面を併せて示し、第4図は本発明に係る温度制
御方法及び装置が好適に使用されるカラー鋼板製
造用の塗料焼付炉の概略構成を示す縦断面図であ
る。
10…熱処理炉、12…高温気体供給管、14
…隔壁、16…バイパス管路、18…熱交換管
路、20…熱交換器、22…開閉蓋、24…加熱
装置、26…温度検出器、28…流量制御弁、3
0…熱処理炉(塗料焼付炉)、32…気体加熱装
置、34…高温気体供給管、36…気体吸引管、
38…吸引送風機、40…隔壁、42…バイパス
管路、44…熱交換器、46…熱交換管路、48
…開閉蓋、50…作動杆、52…アクチユエー
タ、54…温度検出器、56…測温プローブ、5
8…温度制御回路、60…流量制御弁、62…ア
クチユエータ、64…温度制御回路、66,68
…プレナムチヤンバ、70…鋼板、72…ノズ
ル、74,76…ダクト、78…送風機、80…
吸気口、82…コータ、84…強制空冷室、86
…水冷室、88…熱風乾燥装置、90…バーナ。
1 and 2 are schematic configuration diagrams of a temperature control device according to the prior art, and FIG. 3 is a schematic configuration diagram of a temperature control device that can suitably implement the temperature control method according to the present invention. A cross-sectional view of the furnace in the embodiment shown in the figure is also shown, and FIG. 4 is a vertical cross-sectional view showing a schematic configuration of a paint baking furnace for manufacturing color steel sheets in which the temperature control method and device according to the present invention are suitably used. It is. 10... Heat treatment furnace, 12... High temperature gas supply pipe, 14
...Partition wall, 16...Bypass pipe line, 18...Heat exchange pipe line, 20...Heat exchanger, 22...Opening/closing lid, 24...Heating device, 26...Temperature detector, 28...Flow rate control valve, 3
0... Heat treatment furnace (paint baking oven), 32... Gas heating device, 34... High temperature gas supply pipe, 36... Gas suction pipe,
38... Suction blower, 40... Partition wall, 42... Bypass pipe line, 44... Heat exchanger, 46... Heat exchange pipe line, 48
... Opening/closing lid, 50... Operating rod, 52... Actuator, 54... Temperature detector, 56... Temperature measuring probe, 5
8... Temperature control circuit, 60... Flow rate control valve, 62... Actuator, 64... Temperature control circuit, 66, 68
...Plenum chamber, 70... Steel plate, 72... Nozzle, 74, 76... Duct, 78... Blower, 80...
Intake port, 82...Coater, 84...Forced air cooling chamber, 86
...Water cooling room, 88...Hot air dryer, 90...Burner.
Claims (1)
度差を生じさせた気体とを気体混合手段42,4
6,48を介して熱風循環式熱処理炉30に供給
するに際し、前記温度差のある両気体の混合比が
一定になるよう前記気体混合手段42,46,4
8の混合比調節手段48を制御した後、前記気体
混合手段42,46,48に供給される高温気体
の流量を制御し、前記熱風循環式熱処理炉30の
炉内温度が安定した後、その炉内温度を検出して
前記気体混合手段42,46,48の混合比調節
手段48を制御して、前記温度差のある両気体の
混合比を変化させる ことを特徴とする熱風循環式熱処理炉の温度制御
方法。 2 熱風循環式熱処理炉30に高温気体供給管3
4を接続し、この高温気体供給管34の管路の一
部をバイパス管路42と熱交換管路46とに画成
し、前記両管路42,46における高温気体入口
側の連通開口部に各管路42,46の開口比率を
調節可能な開閉蓋48を設け、前記両管路42,
46の高温気体入口側と連通する前記高温気体供
給管34に流量制御弁60を介挿し、更に前記熱
処理炉30に炉内温度検出器54を配設して、こ
れによる検出温度に応じて前記開閉蓋48または
流量制御弁60の開度を選択的に制御するよう構
成した ことを特徴とする熱風循環式熱処理炉の温度制御
装置。[Scope of Claims] 1. A high-temperature gas and a gas in which a temperature difference is generated by heat-exchanging a part of the high-temperature gas are mixed by gas mixing means 42, 4.
The gas mixing means 42, 46, 4 is supplied to the hot air circulation type heat treatment furnace 30 via the gases 6, 48 so that the mixing ratio of the two gases having the temperature difference becomes constant.
After controlling the mixing ratio adjusting means 48 of No. 8, the flow rate of the high temperature gas supplied to the gas mixing means 42, 46, 48 is controlled, and after the temperature inside the hot air circulating heat treatment furnace 30 is stabilized, the A hot air circulation type heat treatment furnace characterized in that the temperature inside the furnace is detected and the mixing ratio adjusting means 48 of the gas mixing means 42, 46, 48 is controlled to change the mixing ratio of the two gases having the temperature difference. temperature control method. 2 High temperature gas supply pipe 3 to hot air circulation heat treatment furnace 30
4, a part of the high temperature gas supply pipe 34 is defined as a bypass pipe 42 and a heat exchange pipe 46, and a communication opening on the high temperature gas inlet side of both the pipes 42 and 46 is formed. is provided with an opening/closing lid 48 that can adjust the opening ratio of each of the pipes 42, 46.
A flow rate control valve 60 is inserted in the high temperature gas supply pipe 34 communicating with the high temperature gas inlet side of the heat treatment furnace 30, and a furnace temperature detector 54 is further provided in the heat treatment furnace 30. A temperature control device for a hot air circulation type heat treatment furnace, characterized in that it is configured to selectively control the opening degree of an opening/closing lid 48 or a flow rate control valve 60.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21167081A JPS58117836A (en) | 1981-12-30 | 1981-12-30 | Method and device for controlling temperature of hot air circulation type heat treating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21167081A JPS58117836A (en) | 1981-12-30 | 1981-12-30 | Method and device for controlling temperature of hot air circulation type heat treating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58117836A JPS58117836A (en) | 1983-07-13 |
| JPH0335989B2 true JPH0335989B2 (en) | 1991-05-30 |
Family
ID=16609643
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21167081A Granted JPS58117836A (en) | 1981-12-30 | 1981-12-30 | Method and device for controlling temperature of hot air circulation type heat treating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58117836A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63134079A (en) * | 1986-11-25 | 1988-06-06 | Nisshin Steel Co Ltd | Paint baking method for painted steel sheet |
-
1981
- 1981-12-30 JP JP21167081A patent/JPS58117836A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58117836A (en) | 1983-07-13 |
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