JPH05357B2 - - Google Patents

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Publication number
JPH05357B2
JPH05357B2 JP63034692A JP3469288A JPH05357B2 JP H05357 B2 JPH05357 B2 JP H05357B2 JP 63034692 A JP63034692 A JP 63034692A JP 3469288 A JP3469288 A JP 3469288A JP H05357 B2 JPH05357 B2 JP H05357B2
Authority
JP
Japan
Prior art keywords
furnace
firing
cooling
present
combustion gas
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 - Lifetime
Application number
JP63034692A
Other languages
Japanese (ja)
Other versions
JPH01212281A (en
Inventor
Satoshi Taniguchi
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP63034692A priority Critical patent/JPH01212281A/en
Publication of JPH01212281A publication Critical patent/JPH01212281A/en
Publication of JPH05357B2 publication Critical patent/JPH05357B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はセラミツク製品の焼成等に用いられる
均熱焼成法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a soaking method for firing ceramic products.

(従来の技術) セラミツク製品焼成を行うにあたり、第5図に
示すように炉体20の下部の対向位置に多数のバ
ーナー21,22を設けておき、これらのバーナ
ー21,22から炉内に高温の燃焼ガス30を噴
射し、天井の排気孔23から排気しつつ焼成する
方法は広く知られている。第5図はこのような従
来法をトンネル炉に利用した例を示すもので、第
5図Aは焼成帯を示し、第5図Bは冷却帯を示し
ている。ところがこのような従来法は、焼成帯で
はバーナー21,22からの燃焼ガスが衝突した
位置に生ずる上昇流の方向とガスの浮力の方向と
が一致し、浮力が上昇流形成を促進する効果を持
つものの、冷却帯ではバーナー21,22から炉
内雰囲気よりも低温のガスが噴出されるため、浮
力は下向きに作用して炉内における上昇流の形成
を阻害するという欠点があつた。このため焼成帯
では炉内に良好な循環流が形成されて炉内雰囲気
が均一に保たれるものの、冷却帯では炉内の循環
が十分には行われず、冷却むらを生じ易かつた。
(Prior Art) When firing a ceramic product, as shown in FIG. A method of firing while injecting combustion gas 30 and exhausting it from the exhaust hole 23 in the ceiling is widely known. FIG. 5 shows an example in which such a conventional method is applied to a tunnel furnace. FIG. 5A shows a firing zone, and FIG. 5B shows a cooling zone. However, in this conventional method, in the firing zone, the direction of the upward flow generated at the location where the combustion gases from the burners 21 and 22 collide coincides with the direction of the buoyancy of the gas, and the buoyancy has an effect of promoting the formation of the upward flow. However, since the burners 21 and 22 blow out gas at a lower temperature than the atmosphere in the furnace in the cooling zone, the buoyant force acts downward and inhibits the formation of an upward flow in the furnace. For this reason, although a good circulation flow is formed in the furnace in the firing zone and the atmosphere in the furnace is kept uniform, in the cooling zone the circulation in the furnace is not sufficiently performed and uneven cooling tends to occur.

(発明が解決しようとする課題) 本発明は上記したような従来の問題点を解決し
て、焼成時のみならず冷却時にも炉内に均一な循
環流を形成することにより焼成むらや冷却むらの
発生を防止することができる均熱焼成法を目的と
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-mentioned conventional problems and eliminates uneven firing and cooling by forming a uniform circulating flow in the furnace not only during firing but also during cooling. This method was developed with the aim of creating a uniform heating method that can prevent the occurrence of

(課題を解決するための手段) 本発明は焼成時には炉体下部の両側対向位置に
設けられた複数のバーナーから炉内におけるガス
の衝突位置が炉幅方向に移動するよう噴出速度を
周期的に変化させつつ燃焼ガスを噴出し上部から
排気しつつ焼成を行い、冷却時には炉体上部の両
側対向位置に設けられた複数のバーナーから同様
に噴出速度を周期的に変化させつつ燃焼ガスを噴
出し下部から排気しつつ冷却を行うことを特徴と
するものである。
(Means for Solving the Problems) The present invention periodically adjusts the jetting speed during firing so that the collision position of gas in the furnace moves in the width direction of the furnace from a plurality of burners installed at opposing positions on both sides of the lower part of the furnace body. Firing is performed while ejecting combustion gas from the top while changing the ejection speed, and during cooling, combustion gas is ejected from multiple burners installed on opposing sides on both sides of the upper part of the furnace body while periodically changing the ejection speed. It is characterized by cooling while exhausting air from the bottom.

(実施例) 以下に本発明をトンネル炉に適用した図示の実
施例とともに更に詳細に説明する。第1図A,B
はそれぞれ焼成帯と冷却帯を示した断面図で、1
はトンネル炉の炉体、2は台車、3は炉体1の天
井に形成されたダンパー4付きの排気孔である。
第1図Aに示されるように、焼成帯の炉体1には
下部両側に複数のバーナー5,6が対向させて設
けられており、各バーナー5,6から高温の燃焼
ガスが矢印のように噴出される。噴出された燃焼
ガスはその衝突位置において上昇流を生じ、天井
の排気孔3から排気される。このとき燃焼ガスは
炉内の雰囲気よりも高温であるから上向きの浮力
を生ずるが、この浮力の方向は上昇流の方向と同
一であるから焼成帯の内部には良好な循環流が形
成される。しかも本発明においてはバーナー5と
バーナー6からの燃焼ガスの噴出速度を周期的に
変化させることにより、ガスの衝突位置、即ち上
昇流の形成される位置を炉幅方向に周期的に移動
させる。この状態は第2図に概略的に示すとおり
であり、第2図イはバーナー6からの噴出速度を
バーナー5からの噴出速度よりも大きくし、炉内
の左側部分に上昇流を形成した状態を、第2図ハ
はその逆の状態を、第2図ロは両者の中間状態を
示している。なおいずれの状態においてもバーナ
ー5からの噴出ガス量とバーナー6からの噴出ガ
ス量の和は一定に保たれるものとする。このよう
にして上昇流の形成位置は炉幅方向に周期的に移
動され、これによつて炉内の温度分布はより一層
均一化されることとなる。
(Example) The present invention will be described in more detail below along with an illustrated example in which the present invention is applied to a tunnel furnace. Figure 1 A, B
1 are cross-sectional views showing the firing zone and cooling zone, respectively.
2 is a furnace body of a tunnel furnace, 2 is a truck, and 3 is an exhaust hole with a damper 4 formed in the ceiling of the furnace body 1.
As shown in FIG. 1A, a plurality of burners 5 and 6 are provided facing each other on both sides of the lower part of the furnace body 1 of the firing zone, and high-temperature combustion gas is emitted from each burner 5 and 6 as shown by the arrows. It is squirted. The ejected combustion gas generates an upward flow at the collision position and is exhausted from the exhaust hole 3 in the ceiling. At this time, the combustion gas has a higher temperature than the atmosphere in the furnace, so it produces an upward buoyant force, but since the direction of this buoyant force is the same as the direction of the upward flow, a good circulating flow is formed inside the firing zone. . Moreover, in the present invention, by periodically changing the ejection speed of the combustion gas from the burners 5 and 6, the gas collision position, that is, the position where the upward flow is formed, is periodically moved in the furnace width direction. This state is schematically shown in Fig. 2, and Fig. 2A shows a state in which the ejection velocity from burner 6 is higher than the ejection velocity from burner 5, and an upward flow is formed in the left part of the furnace. , FIG. 2C shows the opposite state, and FIG. 2B shows an intermediate state between the two. It is assumed that in any state, the sum of the amount of gas ejected from burner 5 and the amount of gas ejected from burner 6 is kept constant. In this way, the position where the upward flow is formed is periodically moved in the width direction of the furnace, thereby making the temperature distribution in the furnace even more uniform.

また第1図Bに示されるように、本発明におい
ては冷却帯の炉体1には上部の両側対向位置に複
数のバーナー7,8が設けられるとともに炉体1
の下部両側には排気管9,10を設けておく。そ
してこれらのバーナー7,8からも上記と同様に
燃焼ガスが噴出され、衝突位置において図示のよ
うな下降流が形成される。前述したように冷却帯
においては炉内雰囲気よりも低温の燃焼ガスが噴
出されるため、浮力は下向きに作用することとな
り、この下降流の方向と一致する。このため本発
明によれば冷却帯の内部にも良好な循環流が形成
される。しかも冷却帯においてもバーナー7とバ
ーナー8からの燃焼ガスの噴出速度は周期的な変
化を与えられ、下降流が形成される衝突位置を炉
幅方向に周期的に変化させるので、冷却帯におけ
る炉内温度分布も均一化され、冷却むらのない均
一な焼成品が得られることとなる。このとき天井
の排気孔さんダンパー4は閉じても良いが、冷却
を促進するために外気の吸引を行わせることもで
きる。
Further, as shown in FIG. 1B, in the present invention, the furnace body 1 of the cooling zone is provided with a plurality of burners 7 and 8 at opposing positions on both sides of the upper part.
Exhaust pipes 9 and 10 are provided on both sides of the lower part. Combustion gas is ejected from these burners 7 and 8 in the same manner as described above, and a downward flow as shown in the figure is formed at the collision position. As mentioned above, in the cooling zone, combustion gas having a lower temperature than the atmosphere in the furnace is ejected, so that the buoyant force acts downward, which corresponds to the direction of this downward flow. Therefore, according to the present invention, a good circulating flow is also formed inside the cooling zone. Moreover, even in the cooling zone, the ejection speed of combustion gas from burners 7 and 8 is periodically changed, and the collision position where the downward flow is formed is periodically changed in the width direction of the furnace. The internal temperature distribution is also made uniform, and a uniform fired product without uneven cooling can be obtained. At this time, the exhaust hole damper 4 on the ceiling may be closed, but outside air may be sucked in to promote cooling.

上記のように本発明においてはバーナー5,6
及び7,8からのガスの噴出速度を周期的に変化
させて衝突位置を炉幅方向に移動させるのである
が、第3図に示されるように炉体1の長手方向に
配置されたバーナーが片側ずつ一斉に同一の変化
を与えられ、衝突位置が炉体1に平行な直線L1
L2,L3上に順次位置するように制御を行うのが
普通である。しかし本発明の他の実施例において
は第4図に示されるように炉体1の長手方向に配
置された各バーナーに個別の変化が与えられ、衝
突位置が炉体1に対して順次角度が変化する直線
L4,L5,L6上に位置するように制御される。
As mentioned above, in the present invention, the burners 5 and 6
The collision position is moved in the width direction of the furnace by periodically changing the ejection speed of the gas from 7 and 8.As shown in FIG. The same change is applied to each side at the same time, and the collision position is a straight line L 1 parallel to the furnace body 1,
Normally, control is performed so that they are located sequentially on L 2 and L 3 . However, in another embodiment of the present invention, as shown in FIG. changing straight line
It is controlled to be located above L 4 , L 5 , and L 6 .

なお以上に説明した実施例はいずれも本発明を
トンネル炉に適用したものであるが、本発明は単
独炉によつても実施することができる。この場合
には炉体1の上下にバーナーを設けておき、焼成
時には下側のバーナーから燃焼ガスを噴出し、冷
却時には上側のバーナーから燃焼ガスを噴出すれ
ばよい。
Although the embodiments described above all apply the present invention to a tunnel furnace, the present invention can also be practiced using a single furnace. In this case, burners may be provided above and below the furnace body 1, and combustion gas may be ejected from the lower burner during firing, and may be ejected from the upper burner during cooling.

(発明の効果) 本発明は以上の実施例による説明からも明らか
なように、焼成時と冷却時とで燃焼ガスの噴出位
置を変えることにより噴出されたガスに作用する
浮力の方向と衝突位置における噴出ガスの流動方
向とを一致させ、炉内に良好な循環流を形成する
ことができるのみならず、燃焼ガスの衝突位置を
炉幅方向に移動させることによつて炉内の温度分
布のより一層の均一化に成功したものである。従
つて本発明によれば焼成時のみならず冷却時にも
炉内の温度分布を均一化することができ、焼成む
らや冷却むらのない焼成品を得ることができる。
よつて本発明は従来の問題点を一掃した均熱焼成
法として、産業の発展に寄与するところ極めて大
である。
(Effects of the Invention) As is clear from the above description of the embodiments, the present invention provides the direction of the buoyant force acting on the ejected gas and the collision position by changing the ejecting position of the combustion gas during firing and cooling. Not only can a good circulation flow be formed in the furnace by aligning the flow direction of the ejected gas in the furnace, but also the temperature distribution in the furnace can be improved by moving the collision position of the combustion gas in the width direction of the furnace. This resulted in further uniformity. Therefore, according to the present invention, the temperature distribution in the furnace can be made uniform not only during firing but also during cooling, and fired products without uneven firing or cooling can be obtained.
Therefore, the present invention greatly contributes to the development of industry as a soaked firing method that eliminates the problems of the conventional method.

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

第1図のA,Bはいずれも本発明の実施例を示
す断面図、第2図のイ,ロ,ハはその作動状態を
示す断面図、第3図はその平面図、第4図は他の
実施例を示す平面図、第5図のA,Bはいずれも
従来例を示す断面図である。 1……炉体、5,6……バーナー、7,8……
バーナー。
A, B in FIG. 1 are sectional views showing an embodiment of the present invention, A, B, and C in FIG. 2 are sectional views showing its operating state, FIG. 3 is a plan view thereof, and FIG. A plan view showing another embodiment, and A and B in FIG. 5 are both sectional views showing a conventional example. 1... Furnace body, 5, 6... Burner, 7, 8...
burner.

【特許請求の範囲】[Claims]

1 加熱すべき試料を瞬間的に加熱する方法にお
いて、該試料をニツケル粉末とチタン粉末から成
る混合圧粉体で包むか又はこれと接触状態にし
て、減圧下で急速に外部加熱することによつて上
記圧粉体に自己発熱反応を誘起させ、該試料に対
して瞬時に外部加熱温度以上の熱を与えることを
特徴とする瞬間加熱方法。
1 In a method of instantaneously heating a sample to be heated, the sample is wrapped in or brought into contact with a mixed compact consisting of nickel powder and titanium powder, and the sample is rapidly externally heated under reduced pressure. An instantaneous heating method characterized by inducing a self-heating reaction in the green compact and instantaneously applying heat higher than an external heating temperature to the sample.

JP63034692A 1988-02-17 1988-02-17 Soaking calcination method Granted JPH01212281A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63034692A JPH01212281A (en) 1988-02-17 1988-02-17 Soaking calcination method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63034692A JPH01212281A (en) 1988-02-17 1988-02-17 Soaking calcination method

Publications (2)

Publication Number Publication Date
JPH01212281A JPH01212281A (en) 1989-08-25
JPH05357B2 true JPH05357B2 (en) 1993-01-05

Family

ID=12421429

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63034692A Granted JPH01212281A (en) 1988-02-17 1988-02-17 Soaking calcination method

Country Status (1)

Country Link
JP (1) JPH01212281A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9073792B2 (en) * 2012-11-13 2015-07-07 Corning Incorporated Methods for improved atmosphere control through secondary gas pressure wave firing

Also Published As

Publication number Publication date
JPH01212281A (en) 1989-08-25

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