JPH06159952A - Batch type baking furnace - Google Patents

Batch type baking furnace

Info

Publication number
JPH06159952A
JPH06159952A JP30992592A JP30992592A JPH06159952A JP H06159952 A JPH06159952 A JP H06159952A JP 30992592 A JP30992592 A JP 30992592A JP 30992592 A JP30992592 A JP 30992592A JP H06159952 A JPH06159952 A JP H06159952A
Authority
JP
Japan
Prior art keywords
furnace
gas
insulating material
differential pressure
atmospheric 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.)
Granted
Application number
JP30992592A
Other languages
Japanese (ja)
Other versions
JP3307697B2 (en
Inventor
Masayoshi Eguchi
雅芳 江口
Fumio Ishida
文雄 石田
Kazuo Iguchi
和夫 井口
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.)
Coorstek KK
Original Assignee
Toshiba Ceramics 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 Toshiba Ceramics Co Ltd filed Critical Toshiba Ceramics Co Ltd
Priority to JP30992592A priority Critical patent/JP3307697B2/en
Publication of JPH06159952A publication Critical patent/JPH06159952A/en
Application granted granted Critical
Publication of JP3307697B2 publication Critical patent/JP3307697B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently purge gas contained in a fibrous insulating material of a furnace by a method wherein a cavity is provided between a casing and the insulating material and an atmospheric gas feed port is opened up to the cavity. CONSTITUTION:When the furnace temperature reaches a heat-treatment temperature, heat-treatment is carried out at this temperature while an atmospheric gas is fed at a specified flow rate for a specified period of time. After that, an on-off valve 7 of an exhaust pipe 8 is opened when the furnace temperature rises further, and an atmospheric gas having a low oxygen concentration is fed into the furnace from an air supply device. However, the supply gas pressure is increased for a specified period of time to purge oxygen contained in a fibrous insulating material 2. After that, the on-off valve 7 is closed and heat- treatment takes place after the gas supply pressure is regulated so that the differential pressure returns to the initial level again. Hereafter, heat treatment is similarly carried out under pre-programed conditions.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ケーシングの内側に繊
維系断熱材を配置し内部に所定の組成の雰囲気ガスを供
給して焼成を行うようにしたバッチ式焼成炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a batch type firing furnace in which a fibrous heat insulating material is placed inside a casing and an atmosphere gas having a predetermined composition is supplied to perform firing.

【0002】[0002]

【従来の技術】従来から、たとえば、Mn・Zn系フェ
ライトのような電子セラミックスや、ファインセラミッ
クスを昇降炉や台車炉のようなバッチ式焼成炉で焼成す
る場合には、焼成温度に応じて雰囲気ガスを酸化雰囲気
から非酸化雰囲気に変えて焼成することが行われてい
る。
2. Description of the Related Art Conventionally, for example, when firing electronic ceramics such as Mn.Zn-based ferrite or fine ceramics in a batch-type firing furnace such as an elevating furnace or a truck furnace, the atmosphere is changed according to the firing temperature. Baking is performed by changing the gas from an oxidizing atmosphere to a non-oxidizing atmosphere.

【0003】このような、雰囲気ガス中の酸素濃度の切
替えは、従来の煉瓦質断熱材を使用したバッチ式焼成炉
の場合には単に供給ガスの組成を変えるだけで比較的容
易に達成できるが、繊維系断熱材を用いたバッチ式焼成
炉の場合には繊維系断熱材中に雰囲気ガスが保有されて
いるため、供給ガスの濃度を変えても繊維系断熱材中に
保有された酸素ガスが徐々に滲み出てくるため応答性が
悪いという問題があり、特に酸素濃度が1000ppm 以下と
非常に低く設定されている場合には所定の酸素濃度にな
るまでに長時間を要するという問題があった。
Such switching of the oxygen concentration in the atmosphere gas can be achieved relatively easily by simply changing the composition of the supply gas in the case of the conventional batch-type firing furnace using a brick heat insulating material. In the case of a batch-type firing furnace that uses a fiber-based heat insulating material, the atmospheric gas is stored in the fiber-based heat insulating material, so even if the concentration of the supply gas is changed, the oxygen gas stored in the fiber-based heat insulating material is changed. However, there is a problem that the responsiveness is poor due to the gradual bleeding, especially when the oxygen concentration is set to a very low value of 1000 ppm or less, it takes a long time to reach the predetermined oxygen concentration. It was

【0004】図2は、このような、従来の円筒型昇降式
バッチ炉を模式的に示す断面図であり、下部開放のケー
シング1の内側に繊維系断熱材2を配置し、下方の開放
部には同様の繊維系断熱材2を上面に配置しその上に支
柱3を介して炉床板4を保持した炉床台車5が嵌合され
るように構成されている。
FIG. 2 is a cross-sectional view schematically showing such a conventional cylindrical lifting type batch furnace, in which a fiber type heat insulating material 2 is arranged inside a casing 1 having a lower opening and a lower opening portion. Is configured so that a similar fibrous heat insulating material 2 is placed on the upper surface thereof, and a hearth trolley 5 holding a hearth plate 4 is fitted thereto via a pillar 3.

【0005】そして、この炉体の上部、側部および下部
には、それぞれガス給気口Gが開口され、また、炉内に
は炉体上部を貫通してヒーター6が挿入され、さらに炉
体上部には開閉弁7を有する排気筒8が開口されてい
る。符号9は端子箱、10は被焼成品である。
Gas inlets G are opened in the upper, side and lower parts of the furnace body, and a heater 6 is inserted through the upper part of the furnace body in the furnace. An exhaust pipe 8 having an opening / closing valve 7 is opened in the upper part. Reference numeral 9 is a terminal box, and 10 is a product to be fired.

【0006】このような従来のバッチ式焼成炉では、上
述した問題を回避するため、オペレーターが経験的に給
気量を調整して雰囲気温度に雰囲気の酸素濃度をマッチ
ングさせていたが、このような方法では、調整に時間が
かかるだけでなく、雰囲気ガスの濃度分布が生じて被焼
成品10近傍の温度と酸素分圧がマッチングせずに焼成
品の歩留まりを低下させるという問題があった。
In such a conventional batch type firing furnace, in order to avoid the above-mentioned problems, the operator empirically adjusts the supply amount to match the oxygen concentration of the atmosphere with the atmospheric temperature. In such a method, there is a problem that not only the adjustment takes time, but also the concentration distribution of the atmospheric gas is generated and the temperature in the vicinity of the article to be fired 10 and the oxygen partial pressure do not match and the yield of the fired article is reduced.

【0007】[0007]

【発明が解決しようとする課題】上述したように従来の
バッチ式焼成炉は、雰囲気調整をオペレーターの経験で
行っていたため、調整に時間がかかるだけでなく、雰囲
気ガスの酸素濃度分布が生じて被焼成品近傍の温度と酸
素濃度がマッチングせずに焼成品の歩留まりを低下させ
るという問題があった。
As described above, in the conventional batch type firing furnace, the atmosphere is adjusted by the experience of the operator, so not only the adjustment takes time, but also the oxygen concentration distribution of the atmosphere gas is generated. There has been a problem that the yield of the fired product is lowered because the oxygen concentration does not match the temperature near the fired product.

【0008】本発明は、かかる従来の問題を解決すべく
なされたもので、炉内雰囲気の組成の変更にあたって繊
維系断熱材に保有された変更前の組成の雰囲気ガスを迅
速にパージすることができ、これによって被焼成品近傍
の温度と雰囲気ガスの組成とのマッチングを短時間に行
わせて、焼成リードタイムを大幅に削減するとともに焼
成品の歩留まりを向上させたバッチ式焼成炉を提供する
ことを目的とする。
The present invention has been made to solve such a conventional problem. When changing the composition of the atmosphere in the furnace, it is possible to quickly purge the atmospheric gas of the composition before the change, which is held in the fiber type heat insulating material. This makes it possible to match the temperature in the vicinity of the product to be fired with the composition of the atmospheric gas in a short time, thereby significantly reducing the firing lead time and providing a batch-type firing furnace in which the yield of fired products is improved. The purpose is to

【0009】[0009]

【課題を解決するための手段】本発明のバッチ式焼成炉
は、ケーシングの内側に繊維系断熱材を配置し内部に所
定の組成の雰囲気ガスを導入して焼成を行うようにした
焼成炉において、前記ケーシングと前記繊維系断熱材と
の間に空隙部を設けて該空隙部に雰囲気ガス給気口を開
口させ、前記雰囲気ガスを前記空隙部から前記繊維系断
熱材を通過させて炉内に供給するよう構成してなること
を特徴としている。
A batch type firing furnace of the present invention is a firing furnace in which a fiber type heat insulating material is arranged inside a casing and an atmosphere gas having a predetermined composition is introduced into the casing for firing. In the furnace, a space is provided between the casing and the fiber-based heat insulating material, an atmosphere gas supply port is opened in the space, and the atmosphere gas is passed from the space through the fiber-based heat insulating material. It is characterized in that it is configured to supply to.

【0010】本発明のバッチ式焼成炉では、雰囲気ガス
の流量を自動制御するために、空隙部と炉内の雰囲気ガ
スの差圧を測定する差圧検出装置と、該差圧検出装置の
出力信号により雰囲気ガスの供給流量を制御する流量制
御装置とを設けることが望ましい。この場合、差圧と繊
維系断熱材の通気抵抗との関係ならびにこの時の最適流
量は予めフィールドで測定して演算装置にインプットし
ておくようにする。
In the batch-type firing furnace of the present invention, in order to automatically control the flow rate of the atmospheric gas, a differential pressure detecting device for measuring the differential pressure between the atmospheric gas in the void and the furnace, and the output of the differential pressure detecting device. It is desirable to provide a flow rate control device that controls the supply flow rate of the atmospheric gas by a signal. In this case, the relationship between the differential pressure and the ventilation resistance of the fiber-based heat insulating material and the optimum flow rate at this time are measured in the field in advance and input to the arithmetic unit.

【0011】さらに、雰囲気ガスの流量を自動制御する
別の手段として、空隙部と炉内に雰囲気ガスの特定の成
分ガス、例えば酸素の差分圧を測定する差分圧検出装置
と、該差分圧検出装置の出力信号により雰囲気ガスの供
給流量を制御する流量制御装置とを設けるようにしても
よい。成分ガスの差分圧を測定する差分圧検出装置とし
ては、例えば、それぞれの位置に酸素濃度を検出する酸
素濃度センサーを配置し、これらのセンサーの差出力か
ら求めるようにしたものが使用できる。
Further, as another means for automatically controlling the flow rate of the atmospheric gas, a differential pressure detecting device for measuring the differential pressure of a specific component gas of the atmospheric gas, for example, oxygen, in the void and the furnace, and the differential pressure detection. A flow rate control device for controlling the supply flow rate of the atmospheric gas according to the output signal of the device may be provided. As the differential pressure detecting device for measuring the differential pressure of the component gas, for example, a device in which an oxygen concentration sensor for detecting the oxygen concentration is arranged at each position and the difference output of these sensors is used can be used.

【0012】この方法で流量制御を行う場合には、直接
に炉内雰囲気が制御されるので、より一層の精密な制御
を行うことができる。
When the flow rate is controlled by this method, the atmosphere in the furnace is directly controlled, so that more precise control can be performed.

【0013】[0013]

【作用】本願発明では、炉内温度が所定の温度になった
ときに雰囲気ガスの組成が変えられるが、このとき雰囲
気ガスが繊維系断熱材中を通過して炉内に供給されてい
るので、繊維系断熱材中に保有されていた前の組成の雰
囲気ガスが効率よくパージされ、かつ、繊維系断熱材の
広い面から供給されるから炉内に雰囲気ガスの濃度分布
が生ずるようなことはない。
In the present invention, the composition of the atmospheric gas is changed when the temperature in the furnace reaches a predetermined temperature. At this time, however, the atmospheric gas passes through the fibrous heat insulating material and is supplied into the furnace. The atmospheric gas of the previous composition contained in the fiber heat insulating material is efficiently purged and is supplied from a wide surface of the fiber heat insulating material, so that the concentration distribution of the atmospheric gas occurs in the furnace. There is no.

【0014】また、雰囲気ガスの切替え時に雰囲気ガス
の供給量を多くするための供給ガスの流量制御装置を設
けた場合には、より短い時間で繊維系断熱材に保有され
たガスのパージを行うことができ、また、精密な雰囲気
ガス組成の調整を行うことができる。
Further, when the supply gas flow rate control device for increasing the supply amount of the ambient gas is provided at the time of switching the ambient gas, the gas retained in the fiber type heat insulating material is purged in a shorter time. In addition, the composition of the atmospheric gas can be precisely adjusted.

【0015】[0015]

【実施例】以下、本発明の実施例について説明する。EXAMPLES Examples of the present invention will be described below.

【0016】図1は、本発明の実施例の円筒型昇降式バ
ッチ炉を示すもので、図2と共通する部分には同一符号
を付してある。
FIG. 1 shows a cylindrical lifting type batch furnace according to an embodiment of the present invention, and the portions common to those in FIG. 2 are designated by the same reference numerals.

【0017】このバッチ炉は、下部開放のケーシング1
の内側に、スタッドボルト11を介してケーシング1と
の間に空隙部Sが形成されるように、ステンレス製の金
網12が配置され、この金網12上に繊維系断熱材2が
固定されている。なお、上部は端子箱9の内側に、ステ
ンレス製の金網12が配置され、この金網12上に繊維
系断熱材2が固定されている。下方の開放部には、内側
に繊維系断熱材2を配置した炉床台車5が嵌合される
が、この繊維系断熱材2も、炉床台車5上にスタッドボ
ルト11を介して空隙部Sが形成されるように配置され
たステンレス製の金網12上に固定されている。また、
炉床台車5上の繊維系断熱材2上には、支柱3を介して
炉床板4が保持されている。
This batch furnace has a casing 1 open at the bottom.
The metal wire mesh 12 made of stainless steel is disposed inside the metal mesh 12 so that a space S is formed between the metal wire mesh 12 and the casing 1 via the stud bolt 11, and the fiber heat insulating material 2 is fixed on the metal wire mesh 12. . A stainless steel wire net 12 is arranged inside the terminal box 9 at the upper part, and the fiber-based heat insulating material 2 is fixed on the wire net 12. A hearth trolley 5 having a fiber-based heat insulating material 2 arranged inside is fitted into the lower open portion. This fiber-based heat insulating material 2 is also provided on the hearth trolley 5 through a stud bolt 11 to form a gap. It is fixed on a stainless steel wire mesh 12 arranged so that S is formed. Also,
A hearth plate 4 is held on the fiber-based heat insulating material 2 on the hearth trolley 5 via columns 3.

【0018】さらに、この炉体の上部、側部および下部
の各空隙部Sには、それぞれガス給気口Gが開口され、
また、炉内には炉体上部を貫通してヒーター6が挿入さ
れ、炉体上部には開閉弁7を有する排気筒8が開口され
ている。
Further, a gas supply port G is opened in each of the upper, side and lower voids S of the furnace body,
Further, a heater 6 is inserted through the upper part of the furnace body in the furnace, and an exhaust pipe 8 having an opening / closing valve 7 is opened in the upper part of the furnace body.

【0019】そして、この実施例においては、炉体の上
部、側部および下部の各空隙部Sに圧力センサ13が配
置され、また、炉内にも、炉床板4近傍に開口する圧力
導入パイプ14が挿入されて、基部には図示を省略した
圧力センサが配置されている。差圧発振器15は、各空
隙部Sの圧力センサ13の圧力と圧力導入パイプ14の
圧力センサの差圧を検出し差圧信号を流量演算装置16
に出力する。流量演算装置15は各ガス給気口Gへ濃度
調整のされた雰囲気ガスを供給する給気装置(マスフロ
ーコントローラー)17を制御するとともに、排気筒8
の開閉を制御する。 なお、図示を省略したが、給気装
置17には窒素ガスボンベと酸素ガスボンベが接続され
て所定の酸素分圧の雰囲気ガスを調整して、この雰囲気
ガスを各ガス給気口Gに供給するようになっており、さ
らに、図示を省略した温度センサにより炉内温度が予め
設定した所定の温度になったときに、酸素分圧の異なる
ガスを調整して各ガス給気口Gに供給するようになって
いる。
In this embodiment, the pressure sensor 13 is arranged in each of the voids S in the upper, side and lower parts of the furnace body, and the pressure introducing pipe opening in the vicinity of the hearth plate 4 is also provided in the furnace. 14 is inserted, and a pressure sensor (not shown) is arranged at the base. The differential pressure oscillator 15 detects the differential pressure of the pressure sensor 13 of each void S and the differential pressure of the pressure sensor of the pressure introducing pipe 14, and outputs a differential pressure signal to the flow rate calculating device 16.
Output to. The flow rate calculation device 15 controls the air supply device (mass flow controller) 17 that supplies the atmosphere gas whose concentration is adjusted to each gas air supply port G, and also the exhaust pipe 8
Control the opening and closing of. Although not shown, a nitrogen gas cylinder and an oxygen gas cylinder are connected to the gas supply device 17 to adjust an atmospheric gas having a predetermined oxygen partial pressure, and the atmospheric gas is supplied to each gas supply port G. Further, when the temperature inside the furnace reaches a predetermined temperature set in advance by a temperature sensor (not shown), gases with different oxygen partial pressures are adjusted and supplied to each gas supply port G. It has become.

【0020】この実施例のバッチ式焼成炉は、次のよう
に用いられる。
The batch type firing furnace of this embodiment is used as follows.

【0021】まず、常法により、炉床板4上に、被焼成
品10、例えばMn・Zn系フェライト部品を、適当な
保持板上に並べて多段に載置し炉本体の下方から挿入す
る。次に、排気筒8の開閉弁7を開放するとともに給気
装置17から酸素濃度の高い雰囲気ガス(窒素ガスと酸
素ガスの混合ガス)が空隙部S内に一定圧力で供給され
る。空隙部Sに供給された雰囲気ガスは、繊維系断熱材
2内を通過して炉内の空気を置換するが、繊維系断熱材
2は通気抵抗を有するので、供給される雰囲気ガスの圧
力は、大気圧よりも高い圧力で炉内に供給される。
First, by a conventional method, the article to be fired 10, for example, Mn.Zn-based ferrite parts are arranged on a suitable holding plate in multiple stages on the hearth plate 4 and inserted from below the furnace body. Next, the open / close valve 7 of the exhaust stack 8 is opened, and the atmosphere gas having a high oxygen concentration (mixed gas of nitrogen gas and oxygen gas) is supplied from the air supply device 17 into the space S at a constant pressure. The atmospheric gas supplied to the void S passes through the inside of the fiber-based heat insulating material 2 to replace the air inside the furnace. However, since the fiber-based heat insulating material 2 has ventilation resistance, the pressure of the supplied atmospheric gas is , Is supplied into the furnace at a pressure higher than atmospheric pressure.

【0022】このとき、差圧発振器15は炉内圧力と空
隙部S内の差圧を検出して差圧信号を流量演算装置16
に出力し、流量演算装置16は所定の差圧となるように
給気装置16に制御信号を供給して一定流量を維持する
ように供給ガス量を調整する。一定の熱処理温度に達す
るとこの温度で所定の時間一定流量で雰囲気ガスが供給
されつつ熱処理が行われる。しかる後、炉温がさらに上
昇されるとともに排気筒8の開閉弁7が開放されて給気
装置17から低酸素濃度の雰囲気ガスが炉内に供給され
るが、このとき繊維系断熱材2に保有されていた酸素を
パージするため、一定時間ガス供給圧力が高くされる。
この後開閉弁7が閉じられて再びもとの差圧となるよう
にガス供給圧力が調整されて熱処理が行われ、以後同様
に予めプログラムされた条件で熱処理が行われる。
At this time, the differential pressure oscillator 15 detects the internal pressure of the furnace and the internal pressure of the void S and outputs a differential pressure signal to the flow rate calculating device 16.
Then, the flow rate calculation device 16 supplies a control signal to the air supply device 16 so as to obtain a predetermined pressure difference, and adjusts the supply gas amount so as to maintain a constant flow rate. When the temperature reaches a constant heat treatment temperature, the heat treatment is performed while the atmospheric gas is supplied at this temperature for a predetermined time at a constant flow rate. After that, the furnace temperature is further increased, the on-off valve 7 of the exhaust stack 8 is opened, and the atmosphere gas having a low oxygen concentration is supplied from the air supply device 17 into the furnace. In order to purge the retained oxygen, the gas supply pressure is raised for a certain period of time.
After that, the on-off valve 7 is closed, the gas supply pressure is adjusted again to the original differential pressure, and the heat treatment is performed. Thereafter, the heat treatment is similarly performed under the pre-programmed conditions.

【0023】ちなみに、この実施例によって、雰囲気ガ
スの酸素濃度を10.000ppm から100ppmに落とした時、パ
ージ時間を従来の 1/5 にすることができた。
By the way, according to this embodiment, when the oxygen concentration of the atmosphere gas was reduced from 10.000 ppm to 100 ppm, the purge time could be reduced to 1/5 of the conventional time.

【0024】なお、以上の実施例では、空隙部Sと炉内
の雰囲気ガスの差圧を測定する差圧検出装置を設け、こ
の差圧検出装置の出力信号により雰囲気ガスの供給流量
を制御するようにした例について説明したが、これに限
らず、例えば、空隙部Sと炉内の雰囲気ガスの特定の成
分ガス、例えば酸素、の差分圧を測定する差分圧検出装
置を設けて、この差分圧検出装置の出力信号により雰囲
気ガスの供給流量を制御するようにしてもよい。
In the above embodiment, a differential pressure detecting device for measuring the differential pressure between the void S and the atmospheric gas in the furnace is provided, and the supply flow rate of the atmospheric gas is controlled by the output signal of this differential pressure detecting device. Although an example of doing so has been described, the present invention is not limited to this, and for example, by providing a differential pressure detection device that measures the differential pressure between the void S and a specific component gas of the atmospheric gas in the furnace, such as oxygen, The supply flow rate of the atmospheric gas may be controlled by the output signal of the pressure detection device.

【0025】この場合、酸素濃度を直接制御できるの
で、より精度の高い雰囲気制御ができ、したがって、焼
成品の歩留まりも一層向上し、焼成リードタイムも大幅
に短縮することができる。
In this case, since the oxygen concentration can be directly controlled, the atmosphere can be controlled with higher accuracy, so that the yield of the fired product can be further improved and the firing lead time can be greatly shortened.

【0026】[0026]

【発明の効果】以上詳述したようにのバッチ式焼成炉を
用いれば、次のように優れた効果を奏することができ
る。
By using the batch type firing furnace as described in detail above, the following excellent effects can be obtained.

【0027】 炉体断熱材に保有されているガスを効
率よくパージすることができる。
The gas held in the furnace body heat insulating material can be efficiently purged.

【0028】 炉内の雰囲気の濃度分布を均一にする
ことができる。
It is possible to make the concentration distribution of the atmosphere in the furnace uniform.

【0029】 雰囲気調整時間を短縮することができ
る。
The atmosphere adjustment time can be shortened.

【0030】また、実施例に示したように、空隙部Sと
炉内の雰囲気ガスの差圧を測定する差圧検出装置や、特
定の成分ガス、例えば酸素、の差分圧を測定する差分圧
検出装置を設けた場合には、操作が非常に容易になるの
で自動化が可能となり、また、雰囲気ガスの使用量も低
減させることができ、さらに、雰囲気ガスの調整が炉体
断熱材の構成に(炉の容積、断熱層厚さ等)左右され
ず、雰囲気の再現性および精度が著しく改善される。
Further, as shown in the embodiment, a differential pressure detecting device for measuring the differential pressure between the void S and the atmosphere gas in the furnace, and a differential pressure for measuring the differential pressure between a specific component gas such as oxygen. When a detection device is provided, the operation is very easy and automation is possible, and the amount of atmospheric gas used can be reduced. The atmosphere reproducibility and accuracy are remarkably improved without being affected by the furnace volume and the thickness of the heat insulating layer.

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

【図1】本発明の円筒型昇降式バッチ炉を模式的に示す
断面図である。
FIG. 1 is a cross-sectional view schematically showing a cylindrical lifting batch furnace of the present invention.

【図2】従来の円筒型昇降式バッチ炉を模式的に示す断
面図である。
FIG. 2 is a cross-sectional view schematically showing a conventional cylindrical lifting type batch furnace.

【符号の説明】[Explanation of symbols]

1……ケーシング、2……繊維系断熱材、3……支柱、
4……炉床板、5……炉床台車、6……ヒーター、7…
…開閉弁、8……排気筒、9……端子箱、10……被焼
成品、11……スタッドボルト、12……金網、13…
…圧力センサ、14……圧力導入パイプ、15……差圧
発振器、16……流量演算装置、17……給気装置、S
……空隙部、G……ガス給気口。
1 ... Casing, 2 ... Fiber insulation, 3 ... Strut,
4 ... hearth plate, 5 ... hearth truck, 6 ... heater, 7 ...
On-off valve, 8 ... Exhaust pipe, 9 ... Terminal box, 10 ... Product to be fired, 11 ... Stud bolt, 12 ... Wire mesh, 13 ...
... pressure sensor, 14 ... pressure introduction pipe, 15 ... differential pressure oscillator, 16 ... flow rate calculation device, 17 ... air supply device, S
…… Void area, G …… Gas inlet.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ケーシングの内側に繊維系断熱材を配置
し内部に所定の組成の雰囲気ガスを導入して焼成を行う
ようにした焼成炉において、前記ケーシングと前記繊維
系断熱材との間に空隙部を設けて該空隙部に雰囲気ガス
給気口を開口させ、前記雰囲気ガスを前記空隙部から前
記繊維系断熱材を通過させて炉内に供給するよう構成し
てなることを特徴とするバッチ式焼成炉。
1. A firing furnace in which a fibrous heat insulating material is disposed inside a casing and an atmosphere gas having a predetermined composition is introduced into the interior of the casing to perform firing, and between the casing and the fibrous heat insulating material. It is characterized in that a void is provided, an atmospheric gas supply port is opened in the void, and the atmospheric gas is passed through the fiber insulating material from the void and supplied into the furnace. Batch type firing furnace.
【請求項2】 前記空隙部と炉内の雰囲気ガスの差圧を
測定する差圧検出装置と、該差圧検出装置の出力信号に
より雰囲気ガスの供給流量を制御する流量制御装置とを
有することを特徴とする請求項1記載のバッチ式焼成
炉。
2. A differential pressure detecting device for measuring a differential pressure between the atmosphere gas in the void and the furnace, and a flow rate control device for controlling a supply flow rate of the atmospheric gas by an output signal of the differential pressure detecting device. The batch type firing furnace according to claim 1, wherein
【請求項3】 前記空隙部と炉内の雰囲気ガスの特定の
成分ガスの差分圧を測定する差分圧検出装置と、該差分
圧検出装置の出力信号により雰囲気ガスの供給流量を制
御する流量制御装置とを有することを特徴とする請求項
1記載のバッチ式焼成炉。
3. A differential pressure detecting device for measuring a differential pressure of a specific component gas of the atmospheric gas in the void and the furnace, and a flow rate control for controlling a supply flow rate of the atmospheric gas by an output signal of the differential pressure detecting device. The batch-type firing furnace according to claim 1, further comprising a device.
JP30992592A 1992-11-19 1992-11-19 Batch type firing furnace Expired - Fee Related JP3307697B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30992592A JP3307697B2 (en) 1992-11-19 1992-11-19 Batch type firing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30992592A JP3307697B2 (en) 1992-11-19 1992-11-19 Batch type firing furnace

Publications (2)

Publication Number Publication Date
JPH06159952A true JPH06159952A (en) 1994-06-07
JP3307697B2 JP3307697B2 (en) 2002-07-24

Family

ID=17998996

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30992592A Expired - Fee Related JP3307697B2 (en) 1992-11-19 1992-11-19 Batch type firing furnace

Country Status (1)

Country Link
JP (1) JP3307697B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018025370A (en) * 2016-08-12 2018-02-15 光洋サーモシステム株式会社 Thermal treatment device
JP2020118446A (en) * 2020-05-15 2020-08-06 光洋サーモシステム株式会社 Thermal treatment device
JP2021073423A (en) * 2020-12-25 2021-05-13 光洋サーモシステム株式会社 Thermal treatment device
KR20220094707A (en) * 2020-12-29 2022-07-06 (주)에코리사이클링 Electric furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018025370A (en) * 2016-08-12 2018-02-15 光洋サーモシステム株式会社 Thermal treatment device
JP2020118446A (en) * 2020-05-15 2020-08-06 光洋サーモシステム株式会社 Thermal treatment device
JP2022074158A (en) * 2020-05-15 2022-05-17 光洋サーモシステム株式会社 Thermal treatment device
JP2021073423A (en) * 2020-12-25 2021-05-13 光洋サーモシステム株式会社 Thermal treatment device
KR20220094707A (en) * 2020-12-29 2022-07-06 (주)에코리사이클링 Electric furnace

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