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JPH0114514B2 - - Google Patents
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JPH0114514B2 - - Google Patents

Info

Publication number
JPH0114514B2
JPH0114514B2 JP55078672A JP7867280A JPH0114514B2 JP H0114514 B2 JPH0114514 B2 JP H0114514B2 JP 55078672 A JP55078672 A JP 55078672A JP 7867280 A JP7867280 A JP 7867280A JP H0114514 B2 JPH0114514 B2 JP H0114514B2
Authority
JP
Japan
Prior art keywords
firing zone
flame firing
furnace
flame
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
Application number
JP55078672A
Other languages
Japanese (ja)
Other versions
JPS576286A (en
Inventor
Ryozo Ban
Takashige Yamauchi
Nobuaki Mori
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.)
Takasago Industry Co Ltd
Original Assignee
Takasago Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Takasago Industry Co Ltd filed Critical Takasago Industry Co Ltd
Priority to JP7867280A priority Critical patent/JPS576286A/en
Publication of JPS576286A publication Critical patent/JPS576286A/en
Publication of JPH0114514B2 publication Critical patent/JPH0114514B2/ja
Granted legal-status Critical Current

Links

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  • Furnace Details (AREA)
  • Tunnel Furnaces (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、酸化焔焼成帯と還元焔焼成帯とが
炉内に連成されたトンネル炉の雰囲気制御方法に
関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to an atmosphere control method for a tunnel furnace in which an oxidizing flame firing zone and a reducing flame firing zone are coupled in the furnace.

従来の技術及び発明が解決しようとする問題点 トンネル炉によつて、例えば、高級白色磁器を
焼成する場合には、1000℃程度まで酸化雰囲気で
加熱した後、還元雰囲気でさらに高温度に加熱す
る必要があり、このような焼成を行なうトンネル
炉は、焼成帯が前半の酸化焔焼成帯と後半の還元
焔焼成帯とに分けられていて、酸化焔焼成帯にお
いては、バーナから燃料が完全燃焼するのに必要
かつ十分な量以上の過剰空気を燃料とともに噴出
して酸化焔焼成帯を形成し、還元焔焼成帯におい
ては、バーナから燃料が完全燃焼するのに必要な
量より少ない空気を燃料とともに噴出してCOガ
ス等の還元ガスを多量に含む還元雰囲気を形成す
るようになつているが、トンネル炉には、搬入口
から焼成帯の最高温度部に向つて温度が次第に上
昇し、最高温度部から搬出口へ向つて次第に温度
が下降する温度勾配を炉内に形成するために、搬
出口側から搬入口側へ向う気流が生ずるように複
数の送風機が配置されているため、酸化焔焼成帯
と還元焔焼成帯の間に何ら仕切手段を設けない
と、上記気流により、還元焔焼成帯から酸化焔焼
成帯へCOガス等の還元性ガスが流入して酸化焔
焼成帯の雰囲気が乱され、焼成した製品の色調が
変化して不良品発生の原因となる。
Problems to be Solved by the Prior Art and the Invention When firing high-grade white porcelain, for example, in a tunnel furnace, it is heated to about 1000°C in an oxidizing atmosphere and then heated to an even higher temperature in a reducing atmosphere. In the tunnel furnace that performs this kind of firing, the firing zone is divided into an oxidizing flame firing zone in the first half and a reducing flame firing zone in the latter half.In the oxidizing flame firing zone, the fuel is completely combusted from the burner. An oxidizing flame firing zone is formed by injecting excess air in excess of the amount necessary and sufficient for complete combustion of the fuel from the burner, and in the reducing flame firing zone, less air than is necessary for complete combustion of the fuel is injected from the burner. However, in a tunnel furnace, the temperature gradually rises from the entrance to the highest temperature part of the firing zone, and the temperature reaches the highest temperature. In order to create a temperature gradient in the furnace in which the temperature gradually decreases from the temperature section to the carry-out port, multiple blowers are arranged to create an airflow from the carry-out port side to the carry-in port side. If no partition means is provided between the firing zone and the reducing flame firing zone, the above airflow will cause reducing gases such as CO gas to flow from the reducing flame firing zone to the oxidizing flame firing zone, and the atmosphere in the oxidizing flame firing zone will change. This will cause the color tone of the fired product to change and lead to defective products.

このため、従来は、酸化焔焼成帯と還元焔焼成
帯の間の壁面に複数の吹込口を形成し、送風機に
より炉外の空気または炉熱を利用して加熱した空
気を噴出口から吹込んで酸化焔焼成帯と還元焔焼
成帯の間を仕切るエアーカーテンを形成し、還元
焔焼成帯から酸化焔焼成帯へCOガス等の還元性
ガスが流入するのを阻止するようになつていた
が、送風機により空気を吹込むため、空気の温度
は数100℃が上限であつて、それ以上の高温度に
することは不可能であり、このような低温度の空
気を吹込むと、その付近の炉内温度が低下し、酸
化焔焼成帯で約1000℃に加熱された被焼成物が急
冷された後、還元焔焼成帯に入つて1000℃以上に
急加熱されることになり、被焼成物に亀裂や割れ
を生ずるおそれがあるばかりでなく、炉内温度を
保つために余分な燃料が必要となつて熱効率が低
下する欠点があり、これを回避するために、空気
の吹込み量を少なくすると、所望の雰囲気を保つ
ことができず、良好な製品を焼成することが困難
となる。
For this reason, conventionally, a plurality of inlets were formed on the wall between the oxidation flame firing zone and the reduction flame firing zone, and air outside the furnace or air heated using the furnace heat was blown in from the jets by a blower. An air curtain was formed between the oxidation flame firing zone and the reduction flame firing zone to prevent reducing gases such as CO gas from flowing from the reduction flame firing zone to the oxidation flame firing zone. Since the air is blown in by a blower, the upper limit of the temperature of the air is several hundred degrees Celsius, and it is impossible to make it higher than that. The temperature inside the furnace decreases, and the object to be fired, which was heated to approximately 1000℃ in the oxidizing flame firing zone, is rapidly cooled, and then enters the reduction flame firing zone where it is rapidly heated to over 1000℃, causing the object to be fired to cool down. Not only is there a risk of cracks and fractures occurring in the furnace, but additional fuel is required to maintain the temperature inside the furnace, which reduces thermal efficiency.To avoid this, it is recommended to reduce the amount of air blown. In this case, it becomes impossible to maintain a desired atmosphere, and it becomes difficult to bake a good product.

本発明はこのような欠点を除去し、炉内温度を
低下させることなく、所望の雰囲気を保つことが
できるようにしたトンネル炉の雰囲気制御方法を
提供することを目的とするものである。
SUMMARY OF THE INVENTION An object of the present invention is to provide an atmosphere control method for a tunnel furnace that eliminates these drawbacks and allows a desired atmosphere to be maintained without lowering the temperature inside the furnace.

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。
Embodiment Hereinafter, an embodiment of the present invention will be described based on the accompanying drawings.

第1図において、1は、内部に左端の搬入口か
ら右端の搬出口に向つて、予熱帯P、焼成帯Q及
び冷却帯Rが順次に形成されたトンネル炉の炉体
であつて、このうち焼成帯Qは、搬入口側の酸化
焔焼成帯Qaと搬出口側の還元焔焼成帯Qbに分け
られており、酸化焔焼成帯Qaには、燃料の完全
燃焼に必要かつ十分な量以上の過剰空気を燃料と
ともに噴出するバーナが炉壁の両側に配置されて
酸化雰囲気を保ち、また、還元焔焼成帯Qbには、
燃料の完全燃焼に必要な量より少ない空気を燃料
とともに噴出するバーナが炉壁の両側に配置され
て還元雰囲気を保つようになつており、酸化焔焼
成帯Qaと還元焔焼成帯Qbとの間の両側の炉壁に
は、第2図に示すように、上下に2個ずつ、合計
4個のバーナ取付孔2が互いに対向して形成され
ており、各バーナ取付孔2には、先拡がりの燃焼
焔噴出口を有するバーナタイル3が嵌着され、そ
の中に、還元焔焼成帯Qbから酸化焔焼成帯Qaへ
流入するCOガス等の未燃焼ガスを完全燃焼させ
るのに十分な量の過剰空気を燃料とともに噴出し
て、燃焼ガスと過剰空気の混合した約1000℃の高
温度のエアーカーテンを酸化焔焼成帯Qaと還元
焔焼成帯Qbの間に形成するバーナ4が装着され
ており、還元焔焼成帯Qbから酸化焔焼成帯Qaに
流入する未燃焼ガスは、バーナ4から噴出する過
剰空気と混合して完全燃焼する。
In FIG. 1, reference numeral 1 denotes a tunnel furnace body in which a pre-heating zone P, a firing zone Q, and a cooling zone R are sequentially formed inside from the carry-in port at the left end to the carry-out port at the right end. Of these, the firing zone Q is divided into an oxidizing flame firing zone Qa on the loading port side and a reducing flame firing zone Qb on the loading port side. Burners that blow out excess air along with fuel are placed on both sides of the furnace wall to maintain an oxidizing atmosphere, and in the reduction flame firing zone Qb,
Burners that eject air with fuel in an amount smaller than that required for complete combustion of the fuel are placed on both sides of the furnace wall to maintain a reducing atmosphere, and between the oxidizing flame firing zone Qa and the reducing flame firing zone Qb. As shown in Fig. 2, a total of four burner mounting holes 2, two on the top and bottom, are formed facing each other in the furnace walls on both sides of the furnace. A burner tile 3 having a combustion flame outlet is fitted in the burner tile 3, and a burner tile 3 is fitted with a burner tile 3 having a sufficient amount to completely burn unburned gas such as CO gas flowing from the reduction flame firing zone Qb to the oxidation flame firing zone Qa. A burner 4 is installed that blows out excess air together with fuel to form a high-temperature air curtain of about 1000°C in which combustion gas and excess air are mixed between the oxidation flame firing zone Qa and the reduction flame firing zone Qb. The unburned gas flowing from the reduction flame firing zone Qb to the oxidation flame firing zone Qa mixes with excess air ejected from the burner 4 and is completely combusted.

発明の構成及び作用効果 上記実施例によつて具体的に説明したように、
本発明のトンネル炉の雰囲気制御方法は、酸化焔
焼成帯と還元焔焼成帯とが炉内に連成されて前記
還元焔焼成帯側から前記酸化焔焼成帯側へ向う気
流が炉内に形成されているトンネル炉の前記酸化
焔焼成帯と前記還元焔焼成帯との間の壁面に配置
したバーナから、前記気流により前記還元焔焼成
帯から前記酸化焔焼成帯へ流入する未燃焼ガスを
略完全に燃焼させるのに十分な量の過剰空気を含
む燃焼ガスを前記酸化焔焼成帯と前記還元焔焼成
帯の間を仕切るエアーカーテン状に噴出すること
を要旨とし、還元焔焼成帯から酸化焔焼成帯へ流
入する未燃焼ガスがバーナから噴出する過剰空気
と混合して略完全燃焼するため、酸化焔焼成帯の
酸化雰囲気が乱されることがなく、炉内温度の低
下を招来しない作用を生じ、焼成した製品の色調
が変化したり、亀裂や割れを生じたりすることが
なく、良好な製品を焼成することができるととも
に、熱効率が向上する効果がある。
Structure and effects of the invention As specifically explained in the above embodiments,
In the tunnel furnace atmosphere control method of the present invention, an oxidizing flame firing zone and a reducing flame firing zone are coupled in the furnace, and an air flow from the reducing flame firing zone side to the oxidizing flame firing zone side is formed in the furnace. Unburnt gas flowing from the reduction flame firing zone to the oxidation flame firing zone by the air flow from a burner disposed on the wall between the oxidation flame firing zone and the reduction flame firing zone of a tunnel furnace where The gist is to eject combustion gas containing a sufficient amount of excess air for complete combustion in the form of an air curtain that partitions the oxidizing flame firing zone and the reducing flame firing zone, Since the unburned gas flowing into the firing zone mixes with the excess air ejected from the burner and burns almost completely, the oxidizing atmosphere in the oxidizing flame firing zone is not disturbed and the furnace temperature does not drop. This has the effect of not only making it possible to bake a good product without changing the color tone of the fired product or causing cracks or cracks, but also improving thermal efficiency.

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

第1図は本発明を実施するトンネル炉の一実施
例の水平断面図、第2図は第1図A−A線拡大断
面図である。 1:炉体、4:バーナ、Qa:酸化焔焼成帯、
Qb:還元焔焼成帯。
FIG. 1 is a horizontal sectional view of an embodiment of a tunnel furnace for implementing the present invention, and FIG. 2 is an enlarged sectional view taken along the line A--A in FIG. 1: Furnace body, 4: Burner, Qa: Oxidation flame firing zone,
Qb: reduction flame firing zone.

Claims (1)

【特許請求の範囲】[Claims] 1 酸化焔焼成帯と還元焔焼成帯とが炉内に連成
されて前記還元焔焼成帯側から前記酸化焔焼成帯
側へ向う気流が炉内に形成されているトンネル炉
の前記酸化焔焼成帯と前記還元焔焼成帯との間の
壁面に配置したバーナから、前記気流により前記
還元焔焼成帯から前記酸化焔焼成帯へ流入する未
燃焼ガスを略完全に燃焼させるのに十分な量の過
剰空気を含む燃焼ガスを前記酸化焔焼成帯と前記
還元焔焼成帯の間を仕切るエアーカーテン状に噴
出することを特徴とするトンネル炉の雰囲気制御
方法。
1. The oxidation flame firing of a tunnel furnace in which an oxidation flame firing zone and a reduction flame firing zone are coupled in the furnace, and an air flow from the reduction flame firing zone side to the oxidation flame firing zone side is formed in the furnace. A burner disposed on the wall between the belt and the reduction flame firing zone generates an amount sufficient to almost completely burn the unburned gas flowing from the reduction flame firing zone to the oxidation flame firing zone by the air flow. A method for controlling an atmosphere in a tunnel furnace, characterized in that combustion gas containing excess air is ejected in the form of an air curtain that partitions the oxidizing flame firing zone and the reducing flame firing zone.
JP7867280A 1980-06-11 1980-06-11 Tunnel furnace Granted JPS576286A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7867280A JPS576286A (en) 1980-06-11 1980-06-11 Tunnel furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7867280A JPS576286A (en) 1980-06-11 1980-06-11 Tunnel furnace

Publications (2)

Publication Number Publication Date
JPS576286A JPS576286A (en) 1982-01-13
JPH0114514B2 true JPH0114514B2 (en) 1989-03-13

Family

ID=13668350

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7867280A Granted JPS576286A (en) 1980-06-11 1980-06-11 Tunnel furnace

Country Status (1)

Country Link
JP (1) JPS576286A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0221187A (en) * 1988-07-09 1990-01-24 Noritake Co Ltd Combustion type continuous calcining tunnel furnace

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50150670A (en) * 1974-05-27 1975-12-03
JPS5650399Y2 (en) * 1977-07-20 1981-11-25

Also Published As

Publication number Publication date
JPS576286A (en) 1982-01-13

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