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JPH0711392B2 - Ceramic firing furnace - Google Patents
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JPH0711392B2 - Ceramic firing furnace - Google Patents

Ceramic firing furnace

Info

Publication number
JPH0711392B2
JPH0711392B2 JP14776789A JP14776789A JPH0711392B2 JP H0711392 B2 JPH0711392 B2 JP H0711392B2 JP 14776789 A JP14776789 A JP 14776789A JP 14776789 A JP14776789 A JP 14776789A JP H0711392 B2 JPH0711392 B2 JP H0711392B2
Authority
JP
Japan
Prior art keywords
ceramic
furnace
fired
firing
furnace body
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
Application number
JP14776789A
Other languages
Japanese (ja)
Other versions
JPH0311286A (en
Inventor
闊 瀬野
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.)
Murata Manufacturing Co Ltd
Original Assignee
Murata Manufacturing 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 Murata Manufacturing Co Ltd filed Critical Murata Manufacturing Co Ltd
Priority to JP14776789A priority Critical patent/JPH0711392B2/en
Publication of JPH0311286A publication Critical patent/JPH0311286A/en
Publication of JPH0711392B2 publication Critical patent/JPH0711392B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Furnace Details (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はマンガン・亜鉛系の電子セラミック材料などの
焼成に使用されるセラミック焼成炉に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a ceramic firing furnace used for firing a manganese-zinc based electronic ceramic material or the like.

[従来の技術] 一般に、マンガン・亜鉛系の電子セラミック材料などの
焼成は、600℃ないし800℃までの昇温過程には、酸化反
応に必要な空気(酸素)を多量に要し、600℃ないし800
℃以降においては、化合物生成のために、酸素分圧が0.
1パーセントないし0.01パーセントとなるように制御し
なければならない。
[Prior Art] Generally, when firing a manganese / zinc-based electronic ceramic material or the like, a large amount of air (oxygen) necessary for the oxidation reaction is required in the temperature rising process from 600 ° C to 800 ° C. Through 800
After ℃, oxygen partial pressure is 0 due to compound formation.
It must be controlled to be 1% to 0.01%.

従来、このような熱処理を必要とするマンガン・亜鉛系
の電子セラミック材料の焼成には、炉本体がトンネル形
状を有する、いわゆるトンネル式の連続焼成炉が使用さ
れていた。この連続焼成炉は、セラミックの被焼成物の
昇温過程で多量の空気(酸素)を投入する領域と、セラ
ミックの被焼成物の焼成過程で雰囲気ガス(窒素)を投
入する領域とに分割されており、熱源としては、電気ヒ
ータが使用されている。この電気ヒータは炉本体内に設
置され、炉本体の一端開口から他端開口に向かって連続
的にプッシュされて炉本体内を連続的に移動する、セラ
ミックの被焼成物を加熱する。
Conventionally, a so-called tunnel-type continuous firing furnace having a furnace body having a tunnel shape has been used for firing the manganese / zinc-based electroceramic material that requires such heat treatment. This continuous firing furnace is divided into a region into which a large amount of air (oxygen) is introduced during the temperature rising process of the ceramic firing object and a region into which an atmospheric gas (nitrogen) is introduced during the firing process of the ceramic firing target. An electric heater is used as a heat source. This electric heater is installed in the furnace main body, and is continuously pushed from one end opening of the furnace main body toward the other end opening to continuously move in the furnace main body to heat a ceramic object to be fired.

[発明が解決しようとする課題] ところで、上記従来のセラミック焼成炉では、600℃な
いし800℃までの昇温過程で空気(酸素)が供給される
ので、この空気の加熱のために多量の熱を電気ヒータか
ら供給しなければならない。また、上記セラミック焼成
炉はトンネル式のものであるので、炉本体の内部空間が
炉本体の両端の開口にて外部に開放されており、600℃
ないし800℃以降で酸素分圧を低く制御するためには、
多量の窒素を必要とする。このため、上記従来のセラミ
ック焼成炉は、使用電気量および使用ガス量が大きく、
非常にランニングコストが高いという問題があった。
[Problems to be Solved by the Invention] In the above-mentioned conventional ceramic firing furnace, since air (oxygen) is supplied during the temperature rising process from 600 ° C to 800 ° C, a large amount of heat is required to heat the air. Must be supplied by an electric heater. Further, since the above ceramic firing furnace is of a tunnel type, the internal space of the furnace body is open to the outside through the openings at both ends of the furnace body, and the temperature is 600 ° C.
Or to control the oxygen partial pressure low after 800 ℃,
Requires a large amount of nitrogen. Therefore, the conventional ceramic firing furnace has a large amount of electricity and gas used,
There was a problem that the running cost was very high.

また、上記従来のセラミック焼成炉は、連続式のもので
あるので、少量多品種のセラミック製品の製造には不向
きであり、しかも、炉本体が両端に開口を有するトンネ
ル状のものであるので、雰囲気制御が難しいという問題
もあった。
Further, since the above-mentioned conventional ceramic firing furnace is a continuous type, it is not suitable for the production of a small amount of a wide variety of ceramic products, and moreover, since the furnace body is a tunnel type having openings at both ends, There was also the problem that it was difficult to control the atmosphere.

本発明の目的は、少量多品種のセラミック製品の製造に
適したランニングコストの低い、省エネルギー型のセラ
ミック焼成炉を提供することである。
An object of the present invention is to provide an energy-saving ceramic firing furnace which is suitable for the production of a large amount of ceramic products in small quantities and has a low running cost.

[課題を解決するための手段] このため、本発明は、炉床部もしくは側壁部からセラミ
ックの被焼成物を出し入れするようにした竪型の炉本体
を有し、この炉本体内に収容された上記セラミックの被
焼成物の昇温過程では酸素を炉本体内に多量に投入しつ
つ上記セラミックの被焼成物を加熱する一方、上記セラ
ミックの被焼成物の焼成過程では雰囲気ガスを炉本体内
に投入して酸素分圧を制御しつつ上記セラミックの被焼
成物を焼成する焼成炉において、 上記昇温過程で炉本体内に燃焼ガスを供給してセラミッ
クの被焼成物を加熱するガス熱源と、上記焼成過程でセ
ラミックの被焼成物を加熱する電気ヒータ熱源とを備え
たことを特徴としている。
[Means for Solving the Problem] For this reason, the present invention has a vertical furnace main body in which a ceramic object to be fired is put in and taken out from a hearth or a side wall, and is housed in the furnace main body. In the heating process of the ceramic fired object, a large amount of oxygen is introduced into the furnace body to heat the ceramic fired object, while in the firing process of the ceramic fired object, atmospheric gas is fed into the furnace body. In a firing furnace for firing the ceramic object to be fired while controlling the oxygen partial pressure, and a gas heat source for supplying a combustion gas into the furnace body to heat the ceramic object to be fired during the heating process. An electric heater heat source for heating the ceramic object to be fired in the above firing process is provided.

[作用] セラミックの被焼成物の上記昇温および焼成が、閉じた
竪型の炉本体内にて行なわれる。そして、昇温過程にお
いてセラミックの被焼成物の酸化のため供給される多量
の空気(酸素)の加熱に要するエネルギーは、電気より
もエネルギーコストの低い燃焼ガスが使用される。一
方、エネルギー消費が格段に少ない上記焼成過程では、
精密な温度制御が容易な電気ヒータ熱源によりセラミッ
クの被焼成物の焼成が行なわれる。
[Operation] The above-mentioned temperature rise and firing of the object to be fired of the ceramic are performed in the closed vertical furnace body. As the energy required for heating a large amount of air (oxygen) supplied to oxidize the material to be fired of ceramics in the temperature rising process, combustion gas whose energy cost is lower than that of electricity is used. On the other hand, in the above firing process, which consumes significantly less energy,
The object to be fired of ceramic is fired by the heat source of the electric heater whose precise temperature control is easy.

[発明の効果] 本発明によれば、セラミックの被焼成物が閉じた炉本体
内にて焼成され、しかも、多量のエネルギーを必要とす
る昇温過程では、エネルギーコストの低いガス熱源によ
り加熱され、エネルギー消費が少ない焼成過程では、精
密な温度制御が容易な電気ヒータ熱源により加熱される
ので、昇温過程ではセラミックの被焼成物の酸化に必要
な酸素量と加熱に必要な熱量とが安価に迅速かつ均一に
炉本体内に供給することができ、また、焼成過程では、
精密な酸素分圧雰囲気に迅速に精度よく切換ができる。
EFFECTS OF THE INVENTION According to the present invention, a ceramic object to be fired is fired in a closed furnace body, and is heated by a gas heat source having a low energy cost in a heating process requiring a large amount of energy. In the firing process, which consumes less energy, it is heated by an electric heater heat source that allows easy precise temperature control. Therefore, in the heating process, the amount of oxygen required to oxidize the material to be fired in the ceramic and the amount of heat required for heating are inexpensive. Can be quickly and uniformly supplied into the furnace body, and during the firing process,
It is possible to switch to a precise oxygen partial pressure atmosphere quickly and accurately.

また、本発明は、バッチ式のものであるので、セラミッ
ク製品の多品種少量生産にも対応することができる。
Further, since the present invention is of a batch type, it can be applied to the production of various kinds of ceramic products in small quantities.

[実施例] 以下、添付の図面を参照して本発明の実施例を説明す
る。
Embodiments Embodiments of the present invention will be described below with reference to the accompanying drawings.

本発明に係るセラミック焼成炉の一実施例の縦断面を図
に示す。
A longitudinal section of an embodiment of a ceramic firing furnace according to the present invention is shown in the drawing.

上記セラミック焼成炉は、中空の支持台1上に支持され
た竪型の炉本体2を有し、この炉本体2の炉床3が炉本
体2の下部開口2aに対して上下に昇降する炉床昇降式の
ものである。上記炉床3は図示しないスクリユジャッキ
もしくは油圧式のテーブルリフタにより、図において実
線で示すIの位置(匣詰位置)と、点線で示すIIの位置
(匣出し位置)との間で昇降する。
The ceramic firing furnace has a vertical furnace body 2 supported on a hollow support 1, and a furnace floor 3 of the furnace body 2 moves up and down with respect to a lower opening 2a of the furnace body 2. It is a floor lift type. The hearth 3 is moved up and down between an I position (a clogged position) shown by a solid line and a II position (a crawled position) shown by a dotted line in the figure by a screw jack or a hydraulic table lifter (not shown). .

上記炉本体2には、その内部空間4を横断して炉本体2
の内壁間をブリッジするように、複数列の炭化珪素系の
棒状の電気ヒータ5が、上記炉本体2の下から上に間隔
をおいて配置される。そして、上記炉床3がIの位置に
上昇している状態では、炉床3上にてセラミックの被焼
成物(図示せず。)が収容されて多段に積み重ねられた
匣10は、電気ヒータ5の隣り合う列の間に配置される。
また、炉本体2の底壁にはシリコンラバー13aが固定さ
れ、炉床3がIの位置に上昇した状態のとき炉床3側の
L字金具13bがこのシリコンラバー13aと密着し、炉内の
気密性が保たれる。
In the furnace body 2, the furnace body 2 is crossed across the inner space 4.
A plurality of rows of silicon carbide-based rod-shaped electric heaters 5 are arranged at intervals above and below the furnace body 2 so as to bridge the inner walls of the furnace. In the state where the hearth 3 is raised to the position I, the box 10 in which ceramic objects to be fired (not shown) are housed on the hearth 3 and stacked in multiple stages is an electric heater. 5 are arranged between adjacent rows.
Further, a silicon rubber 13a is fixed to the bottom wall of the furnace main body 2, and when the hearth 3 is raised to the position I, the L-shaped metal fitting 13b on the hearth 3 side comes into close contact with the silicon rubber 13a, The airtightness of is maintained.

上記電気ヒータ5の上下方向の間隔dや、水平方向の距
離L、さらには発熱部分の長さは、炉本体2内へのセラ
ミックの被焼成物の充填量により異なる。本実施例で
は、直径が30mmφで長さが1000mmないし1800mmの電気ヒ
ータ5を、炉本体2の上下方向に10本、水平方向に4
列、合計40本使用し、これら電気ヒータ5を8回路独立
制御する構成を有する。
The vertical distance d, the horizontal distance L, and the length of the heating portion of the electric heater 5 vary depending on the filling amount of the ceramic material to be fired in the furnace body 2. In this embodiment, 10 electric heaters 5 having a diameter of 30 mm and a length of 1000 mm to 1800 mm are provided in the furnace body 2 in the vertical direction and 4 in the horizontal direction.
A total of 40 columns are used and these electric heaters 5 are independently controlled by 8 circuits.

上記炉本体2には、その対向する一対の側壁7の各下部
に2個所、合計4個所バーナ口6が設けられる。これら
バーナ口6は、バーナ11に接続される。そして、上記炉
本体12内には、上記各バーナ口6に対向して隔壁8が設
けられる。上記各バーナ口6から炉本体2内に供給され
る燃焼ガスは、上記隔壁8に当たって炉本体2の側壁7
に沿って炉本体2内の炉天井12まで上昇したのち、多段
に積み重ねられた匣10の各列の間を通過し、上記炉床3
に設けられた排ガス排出口9から、炉本体2外に排出さ
れる。この過程で炉本体2内に供給された空気が加熱さ
れ、上記匣10内のセラミックの被焼成物に供給される。
The furnace main body 2 is provided with two burner ports 6 at two locations on each lower part of the pair of side walls 7 facing each other. These burner ports 6 are connected to the burner 11. A partition wall 8 is provided in the furnace body 12 so as to face the burner ports 6. Combustion gas supplied into the furnace body 2 from each of the burner ports 6 hits the partition walls 8 to form side walls 7 of the furnace body 2.
After going up to the furnace ceiling 12 in the furnace main body 2 along the passage, it passes between each row of the boxes 10 stacked in multiple stages,
The gas is discharged to the outside of the furnace main body 2 from the exhaust gas discharge port 9 provided in the. In this process, the air supplied into the furnace body 2 is heated and supplied to the ceramic object to be fired in the box 10.

なお、上記バーナ口6は、一対の上記側壁7の各々につ
いて3個所、合計6個所設けて、隔壁8を千鳥状に配置
するようにしてもよい。
The burner ports 6 may be provided in three places on each of the pair of side walls 7, that is, a total of six places, and the partition walls 8 may be arranged in a staggered manner.

セラミックの被焼成物の焼成過程では、上記バーナ口6
よりの燃焼ガスの供給を止め、図示しないガス供給口よ
り、窒素ガスが炉本体2内に供給される。
In the firing process of the ceramic firing object, the burner port 6 is used.
The supply of combustion gas is stopped, and nitrogen gas is supplied into the furnace body 2 through a gas supply port (not shown).

上記焼成炉では、600℃ないし800℃までの上記昇温過程
においてセラミックの被焼成物の酸化のため供給される
多量の空気(酸素)の加熱に要するエネルギーは、電気
よりもコストの低い燃焼ガスが使用される。一方、エネ
ルギー消費が格段に少ない上記焼成過程では、精密な温
度制御が容易な電気ヒータ5によりセラミックの被焼成
物の焼成が行なわれる。
In the above firing furnace, the energy required for heating a large amount of air (oxygen) supplied for the oxidation of the material to be fired in the ceramic in the temperature rising process from 600 ° C. to 800 ° C. Is used. On the other hand, in the above-mentioned firing process in which the energy consumption is remarkably low, the firing target of the ceramic is fired by the electric heater 5 whose precise temperature control is easy.

これにより、昇温過程ではセラミックの被焼成物の酸化
反応に必要な酸素量と加熱に必要な熱量とが安価に迅速
かつ均一に炉本体内に供給される。また、焼成過程で
は、精密な酸素雰囲気に迅速に精度よく切り換えられ
る。
As a result, in the temperature rising process, the amount of oxygen required for the oxidation reaction of the material to be fired of ceramics and the amount of heat required for heating are rapidly and uniformly supplied to the furnace body at low cost. In the firing process, the oxygen atmosphere can be switched to a precise oxygen atmosphere quickly and accurately.

また、セラミックの被焼成物の昇温過程および焼成過程
が、閉じた竪型の炉本体を有するバッチ炉にて行なわれ
るので、セラミック製品の多品種少量生産も容易に行え
る。
Further, since the temperature raising process and the firing process of the ceramic firing object are performed in a batch furnace having a closed vertical furnace body, it is possible to easily produce a large variety of ceramic products in small quantities.

本発明は、炉床昇降式のセラミック焼成炉のほかに、炉
本体の壁面に匣を出し入れするための扉を有するものに
も適用することができる。
The present invention can be applied not only to a hearth elevating and lowering type ceramic firing furnace, but also to a furnace having a door for taking in and out a box on the wall surface of the furnace body.

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

図は本発明に係るセラミック焼成炉の一実施例の縦断面
図である。 2……炉本体、2a開口、3……炉床、5……電気ヒー
タ、6……バーナ口、7……側壁、8……隔壁、9……
排ガス排出口、10……匣、11……バーナ、12……炉天
井。
FIG. 1 is a vertical sectional view of an embodiment of a ceramic firing furnace according to the present invention. 2 ... furnace body, 2a opening, 3 ... hearth, 5 ... electric heater, 6 ... burner port, 7 ... side wall, 8 ... bulkhead, 9 ...
Exhaust gas exhaust port, 10 …… box, 11 …… burner, 12 …… furnace ceiling.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】炉床部もしくは側壁部からセラミックの被
焼成物を出し入れするようにした竪型の炉本体を有し、
この炉本体内に収容された上記セラミックの被焼成物の
昇温過程では酸素を炉本体内に多量に投入しつつ上記セ
ラミックの被焼成物を加熱する一方、上記セラミックの
被焼成物の焼成過程では雰囲気ガスを炉本体内に投入し
て酸素分圧を制御しつつ上記セラミックの被焼成物を焼
成する焼成炉において、 上記昇温過程で炉本体内に燃焼ガスを供給してセラミッ
クの被焼成物を加熱するガス熱源と、上記焼成過程でセ
ラミックの被焼成物を加熱する電気ヒータ熱源とを備え
たことを特徴とするセラミック焼成炉。
1. A vertical furnace body for loading and unloading a ceramic object to be fired from a hearth or a side wall,
In the process of raising the temperature of the material to be fired of the ceramic housed in the furnace body, while heating the material to be fired of the ceramic while introducing a large amount of oxygen into the body of the furnace, the process of firing the material to be fired of the ceramic In a firing furnace in which an atmosphere gas is introduced into the furnace body to control the oxygen partial pressure to fire the ceramic object to be fired, the combustion gas is supplied into the furnace body in the temperature rising process to fire the ceramic object to be fired. A ceramic firing furnace, comprising: a gas heat source for heating an object; and an electric heater heat source for heating a ceramic object to be fired in the firing process.
JP14776789A 1989-06-08 1989-06-08 Ceramic firing furnace Expired - Fee Related JPH0711392B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14776789A JPH0711392B2 (en) 1989-06-08 1989-06-08 Ceramic firing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14776789A JPH0711392B2 (en) 1989-06-08 1989-06-08 Ceramic firing furnace

Publications (2)

Publication Number Publication Date
JPH0311286A JPH0311286A (en) 1991-01-18
JPH0711392B2 true JPH0711392B2 (en) 1995-02-08

Family

ID=15437716

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14776789A Expired - Fee Related JPH0711392B2 (en) 1989-06-08 1989-06-08 Ceramic firing furnace

Country Status (1)

Country Link
JP (1) JPH0711392B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3712715A1 (en) * 2019-03-18 2020-09-23 Montres Breguet S.A. Watch case comprising a rotating bezel

Also Published As

Publication number Publication date
JPH0311286A (en) 1991-01-18

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