JPH0553535B2 - - Google Patents
Info
- Publication number
- JPH0553535B2 JPH0553535B2 JP22548187A JP22548187A JPH0553535B2 JP H0553535 B2 JPH0553535 B2 JP H0553535B2 JP 22548187 A JP22548187 A JP 22548187A JP 22548187 A JP22548187 A JP 22548187A JP H0553535 B2 JPH0553535 B2 JP H0553535B2
- Authority
- JP
- Japan
- Prior art keywords
- flame zone
- burner
- temperature
- furnace
- reduction
- 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 - Fee Related
Links
- 230000003647 oxidation Effects 0.000 claims description 12
- 238000007254 oxidation reaction Methods 0.000 claims description 12
- 239000000446 fuel Substances 0.000 claims description 9
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 5
- 230000001590 oxidative effect Effects 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J6/00—Heat treatments such as Calcining; Fusing ; Pyrolysis
- B01J6/001—Calcining
- B01J6/002—Calcining using rotating drums
Landscapes
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は酸化焔帯と還元焔帯とを備えたトンネ
ル窯の燃焼制御方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a combustion control method for a tunnel kiln equipped with an oxidizing flame zone and a reducing flame zone.
(従来の技術)
陶磁器あるは釉薬瓦等の焼成に用いられるトン
ネル窯には入口側から酸化焔帯と還元焔帯が順次
設けられており、炉内ガスは還元焔帯から酸化焔
帯に向つて流れるため、その境界部分には過剰の
空気を吹込むことによりCOガス等を完全燃焼さ
せるためのバーナが設けられている。ところがこ
のようなトンネル窯は炉内温度のみならず雰囲気
をも適正に制御しなければならぬため、従来は酸
化焔帯と還元焔帯との境界部分にCO計を設置し、
この部分のCO濃度がゼロとなるように還元焔帯
のバーナや過剰の空気を吹込むためのバーナ等を
制御する方法が採用されていた。しかしこれらの
バーナを制御すると炉内温度もこれにつれて変化
するため、炉内雰囲気と炉内温度との両者の変動
の見極めは容易ではなく、オプレータが経験に基
いて各部の制御を行つているのが実状であつて変
動に応じたタイムリーな処置ができないケースも
多かつた。(Conventional technology) A tunnel kiln used for firing ceramics or glazed tiles, etc. is equipped with an oxidation flame zone and a reduction flame zone sequentially from the entrance side, and the gas in the furnace is directed from the reduction flame zone to the oxidation flame zone. A burner is installed at the boundary to blow in excess air to completely burn the CO gas and other gases. However, in such a tunnel kiln, not only the temperature inside the furnace but also the atmosphere must be properly controlled, so conventionally a CO meter was installed at the boundary between the oxidation flame zone and the reduction flame zone.
A method was used to control the reduction flame zone burner and the burner for blowing in excess air so that the CO concentration in this area was zero. However, when these burners are controlled, the temperature inside the furnace changes accordingly, so it is not easy to judge the fluctuations in both the atmosphere inside the furnace and the temperature inside the furnace. However, in many cases, it was not possible to take timely measures in response to changes.
(発明が解決しようとする問題点)
本発明は上記のような従来の問題点を解決し
て、酸化焔帯と還元焔帯とを備えたトンネル窯の
温度と雰囲気とを適切に制御することができるト
ンネル窯の燃焼制御方法を目的として完成された
ものである。(Problems to be Solved by the Invention) The present invention solves the above conventional problems and appropriately controls the temperature and atmosphere of a tunnel kiln equipped with an oxidation flame zone and a reduction flame zone. This was completed with the aim of creating a combustion control method for tunnel kilns that would enable combustion.
(問題点を解決するための手段)
本発明は酸化焔帯と還元焔帯との境界部分に設
けられた空気専用バーナの付近の炉内温度を測定
し、この部分の炉内温度が一定となるように還元
焔帯の後部の燃料専用バーナの出力を調節するこ
とを特徴とするものである。(Means for solving the problem) The present invention measures the furnace temperature near the air-only burner provided at the boundary between the oxidation flame zone and the reduction flame zone, and ensures that the furnace temperature in this area is constant. This is characterized by adjusting the output of the fuel-dedicated burner at the rear of the reduction flame zone so that
以下に本発明を図面を参照しつつ更に詳細に説
明すると、1はトンネル窯の炉体であり、その入
口が酸化焔帯2、中央部分が還元焔帯3とされて
いる、酸化焔帯2には通常のバーナが設けられて
いるが、還元焔帯3には多数の空気燃料混合バー
ナ4が設けられており、その空燃比を調節するこ
とによつて図示のようなCO濃度が形成されてい
る。前述したように、トンネル窯においては炉体
1内に被焼成物の移動方向とは逆無きの流れが発
生するため、還元焔帯3から酸化焔帯2に向つて
還元性ガスが流入するおそれがある。そこで酸化
焔帯2と還元焔帯3との境界部分には空気専用バ
ーナ5が設けられ、還元性ガスを完全燃焼させる
ようになつている。 The present invention will be described in more detail below with reference to the drawings. Reference numeral 1 denotes a furnace body of a tunnel kiln, the inlet of which is an oxidation flame zone 2, and the central part an oxidation flame zone 3. is equipped with a normal burner, but the reducing flame zone 3 is equipped with a number of air-fuel mixture burners 4, and by adjusting the air-fuel ratio, the CO concentration as shown in the figure is created. ing. As mentioned above, in the tunnel kiln, a flow occurs in the furnace body 1 that is not opposite to the direction of movement of the materials to be fired, so there is a risk that reducing gas may flow from the reducing flame zone 3 toward the oxidizing flame zone 2. There is. Therefore, an air-only burner 5 is provided at the boundary between the oxidizing flame zone 2 and the reducing flame zone 3 to completely burn the reducing gas.
従来は還元焔帯3にCO計を設置し、CO濃度が
一定となるように燃焼制御が行われていたのであ
るが、本発明においてはCO計は用いず、その代
わりに空気専用バーナ5の付近に温度計6を設置
して、この部分の温度を測定する。そして温度の
測定値はマイクロコンピユータ等の制御器7に取
込まれ、温度が設定値よりも低い場合には還元焔
帯3の後部に設置された燃料専用バーナ8の出力
を増加させ、逆に温度計6の測定値が設定値より
も高い場合には燃料専用バーナ8の出力を減少さ
せるような制御が行われる。即ち、酸化焔帯2と
還元焔帯3との境界部分のCO濃度が上昇すると
いうことは、還元焔帯3における燃料の比率が高
まつたことを意味し、この結果温度計6は設定値
よりも高い温度を測定するはずである。従つてこ
の場合には燃料専用バーナ8の出力を低下させれ
ば、温度のみならずCO濃度も設定値に戻ること
となる。逆にCO濃度が減少するということは燃
料供給不足を意味するから、温度計6は設定値よ
りも低い温度を測定するはずであり、従つてこの
場合には燃料専用バーナ8の出力を増加させれば
温度とCO濃度とは共に上昇して設定値に戻るこ
ととなる。 Conventionally, a CO meter was installed in the reduction flame zone 3 to control combustion so that the CO concentration remained constant, but in the present invention, a CO meter is not used, and instead, a CO meter is installed in the air-only burner 5. A thermometer 6 is installed nearby to measure the temperature of this part. The measured temperature value is then taken into a controller 7 such as a microcomputer, and if the temperature is lower than the set value, the output of the fuel burner 8 installed at the rear of the reduction flame zone 3 is increased; When the measured value of the thermometer 6 is higher than the set value, control is performed to reduce the output of the fuel-only burner 8. In other words, an increase in the CO concentration at the boundary between the oxidation flame zone 2 and the reduction flame zone 3 means that the ratio of fuel in the reduction flame zone 3 has increased, and as a result, the thermometer 6 has reached the set value. It should measure a higher temperature. Therefore, in this case, by reducing the output of the fuel-only burner 8, not only the temperature but also the CO concentration will return to the set value. Conversely, a decrease in CO concentration means a lack of fuel supply, so the thermometer 6 should measure a temperature lower than the set value, so in this case, the output of the fuel-only burner 8 should be increased. If so, both the temperature and CO concentration will rise and return to the set values.
このように、本発明においては還元焔帯3の
CO濃度との関係に着目し、従来のようにCO濃度
を測定することなく、単に酸化焔帯2と還元焔帯
3との境界部分の温度のみによつて燃焼制御を行
うので、制御が簡単でオペレータの個人差が入り
込む余地のない制御が可能であり、また自動化を
図ることも容易である。この結果、トンネル炉内
の温度および雰囲気を極めて安定に制御すること
ができ、焼成品の品質を安定させるうえでも効果
的である。 In this way, in the present invention, the reduced flame zone 3
Focusing on the relationship with CO concentration, combustion control is performed simply based on the temperature at the boundary between oxidation flame zone 2 and reduction flame zone 3, without measuring CO concentration as in conventional methods, making control easy. It is possible to control the system with no room for individual differences among operators, and it is also easy to achieve automation. As a result, the temperature and atmosphere inside the tunnel furnace can be controlled extremely stably, which is also effective in stabilizing the quality of fired products.
(発明の効果)
本発明は以上の説明からも明らかなように、酸
化焔帯と還元焔帯とを備えたンネル窯の温度と雰
囲気とを容易かつ確実に制御することができるも
のであるから、従来の問題点を一掃したトンネル
窯の燃焼制御方法として、産業の発展に寄与する
ところは極めて大である。(Effects of the Invention) As is clear from the above description, the present invention is capable of easily and reliably controlling the temperature and atmosphere of a tunnel kiln equipped with an oxidation flame zone and a reduction flame zone. As a combustion control method for tunnel kilns that eliminates the problems of conventional methods, it will greatly contribute to the development of industry.
図面は本発明の実施例を説明する平面図であ
る。
2:酸化焔帯、3:還元焔帯、5:空気専用バ
ーナ、8:燃焼専用バーナ。
The drawings are plan views illustrating embodiments of the present invention. 2: Oxidation flame zone, 3: Reduction flame zone, 5: Air-only burner, 8: Combustion-only burner.
Claims (1)
られた空気専用バーナ5の付近の炉内温度を測定
し、この部分の炉内温度が一定となるように還元
焔帯3の後部の燃料専用バーナ8の出力を調節す
ることを特徴とするトンネル窯の燃焼制御方法。1. Measure the furnace temperature near the air-only burner 5 provided at the boundary between the oxidation flame zone 2 and the reduction flame zone 3, and adjust the temperature at the rear of the reduction flame zone 3 so that the temperature inside the furnace in this area is constant. A method for controlling combustion in a tunnel kiln, the method comprising: adjusting the output of a burner 8 dedicated to fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22548187A JPS6467242A (en) | 1987-09-09 | 1987-09-09 | Combustion control method for tunnel kiln |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22548187A JPS6467242A (en) | 1987-09-09 | 1987-09-09 | Combustion control method for tunnel kiln |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6467242A JPS6467242A (en) | 1989-03-13 |
| JPH0553535B2 true JPH0553535B2 (en) | 1993-08-10 |
Family
ID=16829999
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22548187A Granted JPS6467242A (en) | 1987-09-09 | 1987-09-09 | Combustion control method for tunnel kiln |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6467242A (en) |
-
1987
- 1987-09-09 JP JP22548187A patent/JPS6467242A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6467242A (en) | 1989-03-13 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |