JPS61190281A - Method of controlling tunnel furnace in reduction baking - Google Patents
Method of controlling tunnel furnace in reduction bakingInfo
- Publication number
- JPS61190281A JPS61190281A JP2884485A JP2884485A JPS61190281A JP S61190281 A JPS61190281 A JP S61190281A JP 2884485 A JP2884485 A JP 2884485A JP 2884485 A JP2884485 A JP 2884485A JP S61190281 A JPS61190281 A JP S61190281A
- Authority
- JP
- Japan
- Prior art keywords
- zone
- furnace
- port side
- loading port
- firing
- 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
Links
Landscapes
- Tunnel Furnaces (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、トンネル状の炉体の長さ方向の中央部に構成
した焼成帯の一部に還元雰囲気に保った還元帯を設けた
トンネル炉の制御方法に関する。[Detailed Description of the Invention] Industrial Application Field The present invention relates to a tunnel furnace in which a reduction zone maintained in a reducing atmosphere is provided in a part of the firing zone formed in the longitudinal center of a tunnel-shaped furnace body. Regarding control method.
従来の技術及び発明が解決しようとする問題点還元焼成
を行なうトンネル炉は、第1図に示すように、一端に被
焼成物の搬入口2を、他端に搬出口3を夫々形成したト
ンネル状の炉体1の長さ方向の中央部に多数のバーナ4
を列設した焼成帯Bを構成するとともに、搬入口2の付
近に設置したブロア5の吸引管6を炉体1内に貫入し、
かつ、搬出口3の付近に設置したブロア7の吐出管8を
炉体1内に貫入して、両ブロア5.7の駆動により、搬
出口3側が高く、搬入口2が低い圧力勾配が形成されて
、炉体1内に搬出口3側から搬入口2側に向かう気流が
生じ、焼成帯Bの搬入口2側には、焼成帯βから流入す
る高温度のガスによって搬入直後の被焼成物を予熱する
予熱帯Aが、また、焼成帯Bの搬出口3側には1.焼成
帯Bにおいて最高温度に加熱された被焼成物を炉外から
吹き込んだ空気によって冷却する冷却帯Cが夫々構成さ
れ、さらに、焼成帯B内には、搬出口3側から搬入口2
側に向かって、中性雰囲気に保った中性帯B1、還元雰
囲気に保った還元帯B2、炉体1に吐出管10を貫入し
たブロア9によって外気を吹き込んで還元帯B2から流
入する還元ガスを完全燃焼させる浄化帯B3及び酸化雰
囲気に保った酸化帯B4に順次に区分されており、各帯
域の雰囲気は、各バーナの空燃比によって決定され、還
元帯B2または中性帯B1が最高温度に保たれている。Problems to be Solved by the Prior Art and the Invention As shown in FIG. 1, a tunnel furnace for reduction firing is a tunnel having an entrance 2 for carrying in the materials to be fired at one end and an exit 3 at the other end. A large number of burners 4 are installed in the longitudinal center of the furnace body 1.
The suction pipe 6 of the blower 5 installed near the entrance 2 is inserted into the furnace body 1,
In addition, the discharge pipe 8 of the blower 7 installed near the carry-out port 3 penetrates into the furnace body 1, and by driving both blowers 5.7, a pressure gradient is created where the pressure gradient is high on the carry-out port 3 side and low at the carry-in port 2. As a result, an airflow is generated in the furnace body 1 from the carry-in port 3 side to the carry-in port 2 side, and the high-temperature gas flowing from the baking zone β causes the fired material to be fired immediately after being carried into the carry-in port 2 side of the firing zone B. There is a preheating zone A for preheating materials, and a 1. In the firing zone B, cooling zones C are formed in which the objects to be fired heated to the maximum temperature are cooled by air blown from outside the furnace.
Toward the sides, there is a neutral zone B1 kept in a neutral atmosphere, a reducing zone B2 kept in a reducing atmosphere, and a reducing gas flowing from the reducing zone B2 by blowing outside air into the furnace body 1 with a blower 9 inserted through a discharge pipe 10. The atmosphere in each zone is determined by the air-fuel ratio of each burner, and the reducing zone B2 or neutral zone B1 has the highest temperature. is maintained.
そして、各帯域毎に炉内温度を検出し、負荷の変動等に
よって基準温度から外れた場合にはバーナ4に供給する
燃料を増減して基準温度に戻すとともに、燃料に比例し
て燃焼空気の供給流量を増減して各バーナ4の空燃比を
一定に保つようになっているが、各バーナの空燃比を一
定に保っても、搬入口2側のブロア5の吸引量及び搬出
口3側のブロア7の吹き込み量が一定であると、各バー
ナ4の燃焼量によって炉内の雰囲気が変化するのであり
、特に、雰囲気の変化が製品の品質に及ぼす影響の大き
い還元帯においては雰囲気の制御を精密に行なう必要が
ある。The furnace temperature is detected for each zone, and if it deviates from the standard temperature due to load fluctuations, the fuel supplied to the burner 4 is increased or decreased to return it to the standard temperature, and the combustion air is increased in proportion to the fuel. The air-fuel ratio of each burner 4 is kept constant by increasing or decreasing the supply flow rate, but even if the air-fuel ratio of each burner is kept constant, the suction amount of the blower 5 on the loading port 2 side and the suction amount of the blower 5 on the loading port 3 side If the blowing amount of the blower 7 is constant, the atmosphere inside the furnace will change depending on the combustion amount of each burner 4, and especially in the reduction zone where changes in the atmosphere have a large effect on the quality of the product, it is important to control the atmosphere. needs to be done precisely.
そこで、本願の出願人は、還元雰囲気濃度の変化に基づ
いて炉体内を排出口側から搬入口側に向って流れる気流
の流量を制御して還元雰囲気濃度を一定に保つ方法を開
発し、特願昭57−224605号として特許出願した
のであって、この制御方法により、従来に比べて還元雰
囲気濃度の安定化を図ることが可能となったのであるが
、その実施にあたっては、還元帯における還元雰囲気濃
度を直接測定し、その結果に基づいて搬入口側からの炉
内ガスの排出量及び/又は搬出口側への空気の供給量を
制御する方法を採用していたため、還元雰囲気濃度の安
定化に対するより高い要求を必ずしも十分に満足するこ
とができなかった。Therefore, the applicant of the present application has developed a method to keep the reducing atmosphere concentration constant by controlling the flow rate of the air flowing inside the furnace from the discharge port side to the delivery port side based on changes in the reducing atmosphere concentration. A patent application was filed as No. 57-224605, and this control method made it possible to stabilize the reducing atmosphere concentration compared to the conventional method. Because the method used was to directly measure the atmospheric concentration and control the amount of gas discharged from the inlet and/or the amount of air supplied to the outlet based on the results, the concentration of the reducing atmosphere remained stable. It has not always been possible to fully satisfy the higher demands for technology.
すなわち、その後の研究により、還元帯の還元雰囲気濃
度を直接測定して炉内を流れる気流を制御すると、時間
的な遅れが生じて、還元雰囲気源3一
度がある程度変゛動することが判明したのである。In other words, subsequent research has revealed that if the air flow in the furnace is controlled by directly measuring the reducing atmosphere concentration in the reducing zone, a time delay will occur and the reducing atmosphere source will fluctuate to some extent. It is.
発明の目的
本発明は、このような研究の結果に、基づいて完成され
たものであって、還元帯における還元雰囲気濃度を極め
て精密に安定化することができる制御方法を提供するこ
とを目的とするものである。Purpose of the Invention The present invention was completed based on the results of such research, and its purpose is to provide a control method that can stabilize the reducing atmosphere concentration in the reduction zone with extreme precision. It is something to do.
実施例
以下、本発明の一実施例を添付図面に基づいて説明する
。EXAMPLE Hereinafter, an example of the present invention will be described based on the accompanying drawings.
還元帯B2の被焼成体aと炉体1の天井面の間に夫々構
成された空間す、cに設けられた温度検出器22と雰囲
気検知管11によって検知された炉内温度とCoガス濃
度が、温度計23とCO分析計12で夫々計測され、′
その計測値が電気信号として演算装置24.15に入力
され、一方の演算装置24の出力信号により、第2図に
示すように、流量制御弁25.26の開度が調整されて
還元帯B2のバーナ4に供給される燃料と空気の流量が
変更されて、炉内の温度を一定に保つように制御される
とともに、燃料の流量計27と空気の流量計28の計測
値が補正演算装置29に入力され、その補正演算装置2
9において、予め入力されていた演算式に基づいて算出
された補正値が他方の演算装置15に入力され、その出
力信号が回転数制御装置20.21に入力され、その出
力によりブロア7.若しくは冷却帯Cの焼成帯B寄りに
設置されて吸引管19を炉体1内に貫入したブロア18
の回転数が変更されて、冷却帯Cから焼成帯Bに流入す
る空気の流量が変化するようになっており、バーナ4の
燃料消費量が増大すると、実際の還元帯B2内の雰囲気
が変化する前に、CO分析計12で検出された実際のC
oガス濃度より高い濃度になったものとして、炉体1内
に空気を吹き込む搬出口3側のブロア7の回転数が上昇
するか、あるいは、炉体内からガスを炉外に排出するブ
ロア18の回転数が低下して冷却帯Cから焼成帯Bに流
入する空気の量が増大し、燃料消費量の増加に伴う還元
帯B2内の余剰のCOガスを燃焼させて、その濃度を下
げ、逆に燃料消費量が減少すると、Coガス濃度が実際
に低下する前に、排出用のブロア18の回転数が上昇す
るか、あるかは、吹き込み用のブロア7の回転数が低下
して、冷却帯Cから焼成帯Bに流入する空気の量が減少
し、燃料消費量の減少に伴う還元帯B2におけるCOガ
ス濃度の低下が補正される方向の制御が行なわれるので
ある。Furnace temperature and Co gas concentration detected by the temperature detector 22 and atmosphere detection tube 11 provided in the spaces C and C respectively formed between the object a to be fired in the reduction zone B2 and the ceiling surface of the furnace body 1 is measured by the thermometer 23 and the CO analyzer 12, respectively, and '
The measured value is input as an electric signal to the calculation device 24.15, and the output signal of one calculation device 24 adjusts the opening degree of the flow rate control valve 25.26 as shown in FIG. The flow rates of fuel and air supplied to the burner 4 are changed to control the temperature in the furnace to be kept constant, and the measured values of the fuel flow meter 27 and the air flow meter 28 are corrected by a calculation device. 29 and its correction calculation device 2
At step 9, the correction value calculated based on the previously input arithmetic expression is input to the other arithmetic unit 15, and its output signal is input to the rotation speed control device 20. Or a blower 18 installed near the firing zone B of the cooling zone C and having the suction pipe 19 penetrated into the furnace body 1.
The rotational speed of the burner 4 is changed to change the flow rate of air flowing into the firing zone B from the cooling zone C, and as the fuel consumption of the burner 4 increases, the actual atmosphere in the reduction zone B2 changes. The actual C detected by the CO analyzer 12 before
Assuming that the concentration has become higher than the o gas concentration, the rotation speed of the blower 7 on the outlet 3 side that blows air into the furnace body 1 increases, or the rotation speed of the blower 18 that discharges gas from the furnace body to the outside of the furnace increases. As the rotational speed decreases, the amount of air flowing from the cooling zone C to the firing zone B increases, and the excess CO gas in the reduction zone B2 due to the increase in fuel consumption is combusted, reducing its concentration, and vice versa. When the fuel consumption decreases, the rotational speed of the exhaust blower 18 increases before the Co gas concentration actually decreases, or the rotational speed of the blowing blower 7 decreases and cooling Control is performed in such a way that the amount of air flowing from zone C into firing zone B is reduced, and the decrease in CO gas concentration in reduction zone B2 due to the decrease in fuel consumption is corrected.
なお、燃料と燃焼用空気が常に比例して制御される場合
には、補正演算装置29にいずれか一方の流量のみを入
力するようにしてもよい。Note that if the fuel and combustion air are always controlled in proportion, only one of the flow rates may be input to the correction calculation device 29.
また、炉体1内を搬出口3側から搬入口2側に向かう気
流の流量の制御は、搬入口2側のブロア5の回転数の制
御によって行なうようにしてもよい。Further, the flow rate of the air flowing from the carry-in port 3 side to the carry-in port 2 side within the furnace body 1 may be controlled by controlling the rotational speed of the blower 5 on the carry-in port 2 side.
発明の構成及び作用効果
上記実施例によって具体的に説明したように、本発明の
トンネル炉の制御方法は、トンネル状の炉体の長さ方向
の中央部にバーナを列設して焼成帯を構成し、かつ、前
記炉体内の圧力を搬出口側が搬入口側より高くなるよう
に保って搬出口側から搬入口側に向かう気流を生じさせ
ることにより、前記焼成帯の搬入口側に予熱帯を、搬出
口側に冷却帯を夫々構成するとともに、前記焼成帯内を
、搬出口側から搬入口側に向って順次に、中性雰囲気に
保った中性帯、還元雰囲気に保った還元帯、炉内へ空気
を吹き込んで前記還元帯から流入する還元ガスを完全燃
焼させる浄化帯及び酸化雰囲気に保った酸化帯に区分し
たトンネル炉において、前記還元帯における燃料及び/
又は燃焼用空気の供給流量の変化に基づいて炉体内を搬
出口側から搬入口側に向かう前記気流の流量を制御する
ことを要旨とするものであって、還元帯内の雰囲気の変
化に先だって、燃料及び/又は燃焼用空気の供給流量の
変化に基づいて炉内の気流を制御するようにしたから、
遅れ時間を生ずることなく、還元帯内の雰囲気を精密に
一定に制御し得る効果を奏する。Structure and Effects of the Invention As specifically explained in the above embodiments, the method for controlling a tunnel furnace of the present invention includes arranging burners in a row in the longitudinal center of a tunnel-shaped furnace body to form a firing zone. A preheating zone is formed on the loading port side of the firing zone by maintaining the pressure inside the furnace body so that the pressure on the loading port side is higher than that on the loading port side and generating an airflow from the loading port side to the loading port side. A cooling zone is formed on the carrying-out port side, and a neutral zone kept in a neutral atmosphere and a reducing zone kept in a reducing atmosphere are arranged in order from the carrying-out port side to the carrying-in port side in the firing zone. , a tunnel furnace divided into a purification zone where air is blown into the furnace to completely burn the reducing gas flowing in from the reduction zone and an oxidation zone where an oxidizing atmosphere is maintained;
Alternatively, the gist is to control the flow rate of the air flow from the carry-out port side to the carry-in port side in the furnace body based on changes in the supply flow rate of combustion air, and the method is to , since the air flow in the furnace is controlled based on changes in the supply flow rate of fuel and/or combustion air,
This provides the effect of precisely controlling the atmosphere within the reduction zone to a constant level without causing any lag time.
第1図は本発明方法の実施に使用するトンネル炉の断面
図に制御回路のブロック図を併記したものであり、第2
図は還元帯における炉体の横断面図に制御回路のブロッ
ク図を併記したものである。
1:炉体 2:搬入口 3:搬出口 4:バーナ 5.
7.9.18ニブロア 11:C○濃度検出管 12
: Co濃度分析計 15.24=演算装置 20.2
1:制御装置 22:温度検出器 23:温度計 25
.26:流量制御弁 27.28二流量計 29=補正
演算装W A:予熱帯 B:焼成体 C:冷却帯 Bl
中性帯 B2:還元帯 B3:浄化帯 B4:酸化帯Figure 1 is a cross-sectional view of a tunnel furnace used to carry out the method of the present invention, together with a block diagram of the control circuit.
The figure shows a cross-sectional view of the furnace body in the reduction zone along with a block diagram of the control circuit. 1: Furnace body 2: Loading port 3: Loading port 4: Burner 5.
7.9.18 Nibloa 11: C○ concentration detection tube 12
: Co concentration analyzer 15.24 = calculation device 20.2
1: Control device 22: Temperature detector 23: Thermometer 25
.. 26: Flow rate control valve 27. 28 Two flow meters 29 = Correction calculation unit W A: Preliminary zone B: Firing body C: Cooling zone Bl
Neutral zone B2: Reduction zone B3: Purification zone B4: Oxidation zone
Claims (1)
て焼成帯を構成し、かつ、前記炉体内の圧力を搬出口側
が搬入口側より高くなるように保って搬出口側から搬入
口側に向かう気流を生じさせることにより、前記焼成帯
の搬入口側に予熱帯を、搬出口側に冷却帯を夫々構成す
るとともに、前記焼成帯内を、搬出口側から搬入口側に
向って順次に、中性雰囲気に保った中性帯、還元雰囲気
に保った還元帯、炉内へ空気を吹き込んで前記還元帯か
ら流入する還元ガスを完全燃焼させる浄化帯及び酸化雰
囲気に保った酸化帯に区分したトンネル炉において、前
記還元帯における燃料及び/又は燃焼用空気の供給流量
の変化に基づいて炉体内を搬出口側から搬入口側に向か
う前記気流の流量を制御することを特徴とする還元焼成
におけるトンネル炉の制御方法A firing zone is formed by arranging burners in the longitudinal center of a tunnel-shaped furnace body, and the pressure inside the furnace body is maintained so that the pressure on the outlet side is higher than that on the carry-in port side. By generating an airflow toward the loading port side, a preheating zone is formed on the loading port side of the firing zone, and a cooling zone is formed on the loading port side, and the inside of the firing zone is moved from the loading port side to the loading port side. In this order, a neutral zone maintained in a neutral atmosphere, a reduction zone maintained in a reducing atmosphere, a purification zone in which air is blown into the furnace to completely burn the reducing gas flowing from the reduction zone, and an oxidizing atmosphere maintained in the furnace. In a tunnel furnace divided into an oxidation zone, the flow rate of the air flow from the outlet side to the inlet side in the furnace body is controlled based on changes in the supply flow rate of fuel and/or combustion air in the reduction zone. Tunnel furnace control method for reduction firing
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2884485A JPS61190281A (en) | 1985-02-16 | 1985-02-16 | Method of controlling tunnel furnace in reduction baking |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2884485A JPS61190281A (en) | 1985-02-16 | 1985-02-16 | Method of controlling tunnel furnace in reduction baking |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61190281A true JPS61190281A (en) | 1986-08-23 |
Family
ID=12259673
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2884485A Pending JPS61190281A (en) | 1985-02-16 | 1985-02-16 | Method of controlling tunnel furnace in reduction baking |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61190281A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59115976A (en) * | 1982-12-20 | 1984-07-04 | 高砂工業株式会社 | Method of controlling tunnel kiln in reduction baking |
-
1985
- 1985-02-16 JP JP2884485A patent/JPS61190281A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59115976A (en) * | 1982-12-20 | 1984-07-04 | 高砂工業株式会社 | Method of controlling tunnel kiln in reduction baking |
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