JPH0526580A - Continuous baking furnace - Google Patents

Continuous baking furnace

Info

Publication number
JPH0526580A
JPH0526580A JP3176493A JP17649391A JPH0526580A JP H0526580 A JPH0526580 A JP H0526580A JP 3176493 A JP3176493 A JP 3176493A JP 17649391 A JP17649391 A JP 17649391A JP H0526580 A JPH0526580 A JP H0526580A
Authority
JP
Japan
Prior art keywords
temperature zone
furnace
low temperature
continuous firing
binder
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.)
Pending
Application number
JP3176493A
Other languages
Japanese (ja)
Inventor
Akira Taguchi
韶 田口
Seigo Ootani
鉦吾 大谷
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.)
Niterra Co Ltd
Original Assignee
NGK Spark Plug 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 NGK Spark Plug Co Ltd filed Critical NGK Spark Plug Co Ltd
Priority to JP3176493A priority Critical patent/JPH0526580A/en
Publication of JPH0526580A publication Critical patent/JPH0526580A/en
Pending legal-status Critical Current

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  • Tunnel Furnaces (AREA)
  • Furnace Charging Or Discharging (AREA)

Abstract

PURPOSE:To obtain a continuous baking furnace capable of discharging binder gas to the outside of the furnace without disturbing temperature distribution in the furnace. CONSTITUTION:The title furnace is provided with a low temperature zone 1, in which binder included in forms 7 not baked yet is evaporated, a middle temperature zone 2, in which the forms 7 not baked yet are preheated, and a high temperature zone 3, in which the forms 7 not baked yet are baked. The title furnace is added with a discharging gas removing mechanism 5, introducing heating air 57 from the upper part of the furnace of the low temperature zone 1 and discharging it through the floor 12 of the furnace.

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、未焼成セラミックを焼
成する際に使用する連続焼成炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous firing furnace used when firing an unfired ceramic.

【0002】[0002]

【従来の技術】低温帯で発生するバインダーガスの吸収
に拠る焼成不良品の発生を防止する為、従来の連続焼成
炉では換気扇を用い、ガスを低温帯から強制排出させて
いる。
2. Description of the Related Art In order to prevent defective firing due to absorption of a binder gas generated in a low temperature zone, a ventilation fan is used in a conventional continuous firing furnace to forcibly discharge the gas from the low temperature zone.

【0003】[0003]

【発明が解決しようとする課題】しかるに、従来の連続
焼成炉は以下の様な欠点がある。バインダーガスの発生
量に応じて換気扇の能力を調節させる必要があり、これ
に伴い炉内には換気能力に応じた気流が発生し、各温度
帯の温度分布が乱れる。本発明の目的は、炉内の温度分
布を乱すことなくバインダーガスを炉外に排出できる連
続焼成炉の提供にある。
However, the conventional continuous firing furnace has the following drawbacks. It is necessary to adjust the capacity of the ventilation fan according to the amount of binder gas generated, and along with this, an air flow according to the ventilation capacity is generated in the furnace, and the temperature distribution in each temperature zone is disturbed. An object of the present invention is to provide a continuous firing furnace capable of discharging the binder gas outside the furnace without disturbing the temperature distribution inside the furnace.

【0004】[0004]

【課題を解決するための手段】上記課題の解決のため、
本発明は、入口近傍に位置し、被焼成成形体に含まれる
バインダーを蒸発させる低温帯と、該低温帯より後方に
位置し、前記低温帯を通過してきた被焼成成形体を予熱
する中温帯と、該中温帯より後方に位置し、前記中温帯
を通過してきた被焼成成形体を焼成する高温帯とを備え
た連続焼成炉において、前記低温帯の炉上部から加熱空
気を導入し炉床部から排気する、排ガス除去機構を付加
した構成を採用した。
[Means for Solving the Problems] In order to solve the above problems,
The present invention is directed to a low temperature zone located near an inlet for evaporating a binder contained in a body to be fired, and a medium temperature zone located behind the low temperature zone for preheating a body to be fired that has passed through the low temperature zone. And a continuous firing furnace that is located behind the intermediate temperature zone and has a high temperature zone for firing the article to be fired that has passed through the intermediate temperature zone, in which heated air is introduced from the furnace upper part of the low temperature zone A structure with an exhaust gas removal mechanism for exhausting from the section was adopted.

【0005】[0005]

【作用】被焼成成形体に含まれるバインダーが低温帯で
蒸発し、バインダーガスが低温帯の炉内に溜まる。排ガ
ス除去機構は、低温帯の炉上部から加熱空気を導入し、
炉床部から排気する(ダンプロー方式)。このため、横
方向の気流の流れが炉内に発生する事無く、バインダー
ガスは炉外に強制的に排出される。
Function: The binder contained in the article to be fired evaporates in the low temperature zone, and the binder gas accumulates in the furnace in the low temperature zone. The exhaust gas removal mechanism introduces heated air from the upper part of the furnace in the low temperature zone,
Exhaust from the hearth (Damplow method). Therefore, the binder gas is forcibly discharged to the outside of the furnace without generating a lateral air flow inside the furnace.

【0006】[0006]

【発明の効果】低温帯の炉上部から加熱空気を導入し、
炉床部から排気する構成であるので炉内横方向に気流が
流れず、炉内の温度分布を乱すことなくバインダーガス
を炉外に排出できる。
EFFECTS OF THE INVENTION Introducing heated air from the upper part of the furnace in the low temperature zone,
Since the gas is exhausted from the furnace floor, the air current does not flow in the lateral direction of the furnace, and the binder gas can be discharged to the outside of the furnace without disturbing the temperature distribution in the furnace.

【0007】[0007]

【実施例】つぎに、本発明の一実施例を図1〜図4に基
づき説明する。図1、図4に示す如く、連続焼成炉A
は、低温帯1、中温帯2、高温帯3、冷却帯4を備え、
バインダーガス10を強制排出する排ガス除去機構5、
および熱気排出機構6を具備する。また、この連続焼成
炉A(全長数十m)は、炉壁が耐火物で形成され、炉床
レール100上に移動自在に配された、耐熱材製の台板
(又は台車)110に未焼成成形体7が載置される。
尚、図示左側の入口130から搬入された未焼成成形体
7は、プッシャー方式で炉内を移動し、図示右側の出口
140から製品として搬出される。
EXAMPLE An example of the present invention will be described below with reference to FIGS. As shown in FIGS. 1 and 4, continuous firing furnace A
Includes a low temperature zone 1, a medium temperature zone 2, a high temperature zone 3, and a cooling zone 4,
Exhaust gas removing mechanism 5 for forcibly discharging the binder gas 10,
And a hot air discharge mechanism 6. Further, in this continuous firing furnace A (total length: several tens of meters), the furnace wall is made of a refractory material, and the base plate (or dolly) 110 made of a heat-resistant material is movably arranged on the hearth rail 100 and is not yet mounted. The fired compact 7 is placed.
The green body 7 carried in through the inlet 130 on the left side of the drawing moves in the furnace by the pusher method and is carried out as a product through the outlet 140 on the right side of the drawing.

【0008】低温帯1は、入口130近傍に位置し、電
熱ヒータ11により、前部が室温、後部が500℃とな
るように温度分布が設定されている。また、この低温帯
1を未焼成成形体7が通過する際、後述する有機バイン
ダーが蒸発する。中温帯2は、低温帯1の後部に位置
し、電熱ヒータ21により、前部が600℃、後部が1
300℃となるように温度分布が設定されている。低温
帯1を通過した未焼成成形体7は、焼成し易い様にこの
中温帯2で予熱される。高温帯3は、中温帯2の後部に
位置し、電熱ヒータ31により、前部が1300℃、後
部が1600℃となるように温度分布が設定されてい
る。低温帯1を通過した未焼成成形体7はこの高温帯3
で焼成される。冷却帯4は、空冷されており、高温帯3
を通過した製品を室温迄冷やす。
The low temperature zone 1 is located in the vicinity of the inlet 130, and the temperature distribution is set by the electric heater 11 such that the front portion has room temperature and the rear portion has 500 ° C. Moreover, when the green body 7 passes through the low temperature zone 1, the organic binder described later evaporates. The middle temperature zone 2 is located at the rear part of the low temperature zone 1, and the front part is 600 ° C. and the rear part is 1 degree by the electric heater 21.
The temperature distribution is set to be 300 ° C. The unsintered compact 7 that has passed through the low temperature zone 1 is preheated in the middle temperature zone 2 so as to be easily sintered. The high temperature zone 3 is located at the rear part of the middle temperature zone 2, and the temperature distribution is set by the electric heater 31 so that the front part becomes 1300 ° C. and the rear part becomes 1600 ° C. The green compact 7 that has passed through the low temperature zone 1 is the high temperature zone 3
Is baked in. The cooling zone 4 is air-cooled, and the high temperature zone 3
The product passed through is cooled to room temperature.

【0009】排ガス除去機構5は、図2にも示す様に、
低温帯1の炉床部12の炉床レール100の側方に形成
された開口120に連通する三本の排気パイプ51(内
径46mm、外径50mmのステンレス)、該パイプ5
1に取付けられた空気量調整バルブ52付きアスピレー
タ53(内径4mm、外径5mmのステンレス)、該ア
スピレータ53に空気54を供給するコンプレッサ55
からなる排気部と、高温帯3から中温帯2の炉外壁に受
熱パイプ56を沿わすことに拠り炉上部13から加熱空
気57を導入する加熱空気導入部とで構成される。な
お、空気量調整バルブ52は、水蒸気センサ81および
二酸化炭素センサ82の各出力が入力される制御装置8
に電気接続され、低温帯1の水蒸気量、二酸化炭素の濃
度が、夫々80%、2%を越えない様に開口具合が操作
される。
The exhaust gas removing mechanism 5 is, as shown in FIG.
Three exhaust pipes 51 (stainless steel having an inner diameter of 46 mm and an outer diameter of 50 mm) communicating with the openings 120 formed on the side of the hearth rail 100 of the hearth portion 12 of the low temperature zone 1, and the pipe 5
1, an aspirator 53 with an air amount adjusting valve 52 (stainless steel having an inner diameter of 4 mm and an outer diameter of 5 mm), and a compressor 55 for supplying air 54 to the aspirator 53.
And a heated air introduction part for introducing heated air 57 from the furnace upper part 13 by arranging the heat receiving pipe 56 along the outer wall of the furnace from the high temperature zone 3 to the medium temperature zone 2. The air amount adjusting valve 52 is a control device 8 to which the outputs of the water vapor sensor 81 and the carbon dioxide sensor 82 are input.
The opening degree is controlled so that the amount of water vapor and the concentration of carbon dioxide in the low temperature zone 1 do not exceed 80% and 2%, respectively.

【0010】熱気排出機構6は、図3にも示す様に、高
温帯3(一部中温帯2)の炉上部に配設された四本の排
熱パイプ61(内径46mm、外径50mmのステンレ
ス)、該パイプ61に取付けられた空気量調整バルブ6
2付きアスピレータ63(内径4mm、外径5mmのス
テンレス)、該アスピレータ63に空気を供給するコン
プレッサ(図示せず)で構成され、空気を含むアルカリ
質ガラスガスを0.5m3 /分〜1.5m3 /分の割合
で炉外に排出する。なお、空気量調整バルブ62は、温
度センサ83、84の出力が入力される制御装置8に電
気接続され、前部、後部温度が著しく変動しないように
開口具合が操作される。
As shown in FIG. 3, the hot air exhaust mechanism 6 includes four exhaust heat pipes 61 (having an inner diameter of 46 mm and an outer diameter of 50 mm) arranged at the upper part of the furnace in the high temperature zone 3 (partially medium temperature zone 2). (Stainless steel), air amount adjusting valve 6 attached to the pipe 61
2 and an aspirator 63 (stainless steel having an inner diameter of 4 mm and an outer diameter of 5 mm) and a compressor (not shown) that supplies air to the aspirator 63, and the alkaline glass gas containing air is 0.5 m 3 / min to 1. Discharge to the outside of the furnace at a rate of 5 m 3 / min. The air amount adjusting valve 62 is electrically connected to the control device 8 to which the outputs of the temperature sensors 83 and 84 are input, and the opening degree is operated so that the front and rear temperatures do not change significantly.

【0011】未焼成成形体7は、アルミナ90重量%、
珪素3.3重量%、酸化カルシウム3重量%、酸化マグ
ネシウム3重量%からなるセラミック素材に、有機バイ
ンダーとして、セルローズ3〜5重量%、パラフィン3
〜5 重量%、水0.5重量%を含有させて所定形状に成
形したものである。
The green compact 7 is made of 90% by weight of alumina,
A ceramic material composed of 3.3% by weight of silicon, 3% by weight of calcium oxide and 3% by weight of magnesium oxide, and 3 to 5% by weight of cellulose and paraffin 3 as an organic binder.
-5% by weight and 0.5% by weight of water are contained to form a predetermined shape.

【0012】つぎに、連続焼成炉Aの作用効果を述べ
る。 (ア)低温帯1のバインダーガス10が効率良く炉外に
排出されるので、製品にキレやブク歪みが発生しない。 (イ)低温帯1の炉床部12から排気し、低温帯1の炉
上部13から加熱空気57を導入してバインダーガス1
0を炉外に排出する構成であるので、低温帯1、中温帯
2、高温帯3の温度分布を乱さない。 (ウ)空気量調整バルブ52の開度具合を変えることに
より、バインダーガス10の排出量を広範囲に可変でき
る。 (エ)熱気排出機構6に拠り、焼成時に発生するアルカ
リ質ガラスガスが短時間に排出され、製品がアルカリ質
ガラスガスで汚れず、電熱ヒータ11、21、31や炉
内壁も傷まない。なお、熱気排出機構6による、空気を
含むアルカリ質ガラスガスの排出は少量(アルカリ質ガ
ラスガスの発生量は少量)であるので、高温帯3に向か
って流れる気流は極僅かであり、炉内の温度分布を著し
く乱すことはない。 (オ)従来の連続炉では排気ダクトに換気扇が配設され
ているのでダクト内に付着したカーボンや未燃焼樹脂の
掃除に手間がかかる。本実施例の連続焼成炉Aでは排気
ダクト50に換気扇が配設されないのでダクト掃除に手
間がかからない。 (カ)高温帯3、中温帯2の排熱を利用して空気を加熱
しているので加熱用のエネルギーを別に用意する必要が
ない。
Next, the function and effect of the continuous firing furnace A will be described. (A) Since the binder gas 10 in the low temperature zone 1 is efficiently discharged to the outside of the furnace, the product is free from cracks and distortion. (A) Exhaust from the hearth 12 of the low temperature zone 1 and introduce heated air 57 from the furnace upper part 13 of the low temperature zone 1 to generate the binder gas 1
Since 0 is discharged to the outside of the furnace, the temperature distribution of the low temperature zone 1, the middle temperature zone 2 and the high temperature zone 3 is not disturbed. (C) By changing the opening degree of the air amount adjusting valve 52, the discharge amount of the binder gas 10 can be varied over a wide range. (D) Due to the hot air discharge mechanism 6, the alkaline glass gas generated during firing is discharged in a short time, the product is not contaminated with the alkaline glass gas, and the electric heaters 11, 21, 31 and the furnace inner wall are not damaged. Since the amount of alkaline glass gas containing air discharged by the hot air discharge mechanism 6 is small (the amount of alkaline glass gas generated is small), the air flow flowing toward the high temperature zone 3 is extremely small, and Does not significantly disturb the temperature distribution of. (E) In the conventional continuous furnace, since the ventilation fan is arranged in the exhaust duct, it takes time and effort to clean the carbon and unburned resin adhering to the inside of the duct. In the continuous firing furnace A of this embodiment, no ventilation fan is provided in the exhaust duct 50, so that cleaning the duct does not take time. (F) Since the air is heated by utilizing the exhaust heat of the high temperature zone 3 and the medium temperature zone 2, it is not necessary to separately prepare energy for heating.

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

【図1】本発明の一実施例である連続焼成炉の構造図で
ある。
FIG. 1 is a structural diagram of a continuous firing furnace that is an embodiment of the present invention.

【図2】その連続焼成炉における排ガス除去機構(一
部)の構造説明図である。
FIG. 2 is a structural explanatory view of an exhaust gas removing mechanism (a part) in the continuous firing furnace.

【図3】その連続焼成炉における熱気排出機構(一部)
の構造説明図である。
FIG. 3 Hot air discharge mechanism in the continuous firing furnace (part)
It is a structure explanatory view of.

【図4】その連続焼成炉の低温帯の断面図である。FIG. 4 is a sectional view of a low temperature zone of the continuous firing furnace.

【符号の説明】[Explanation of symbols]

A 連続焼成炉 1 低温帯 2 中温帯 3 高温帯 5 排ガス除去機構 7 未焼成成形体(被焼成成形体) 12 炉床部 13 炉上部 57 加熱空気 130 入口 A Continuous firing furnace 1 Low temperature zone 2 Medium temperature zone 3 High temperature zone 5 Exhaust gas removal mechanism 7 Unsintered compact (sintered compact) 12 Hearth 13 Upper furnace 57 Heated air 130 Inlet

Claims (1)

【特許請求の範囲】 【請求項1】 入口近傍に位置し、被焼成成形体に含ま
れるバインダーを蒸発させる低温帯と、 該低温帯より後方に位置し、前記低温帯を通過してきた
被焼成成形体を予熱する中温帯と、 該中温帯より後方に位置し、前記中温帯を通過してきた
被焼成成形体を焼成する高温帯とを備えた連続焼成炉に
おいて、 前記低温帯の炉上部から加熱空気を導入し炉床部から排
気する、排ガス除去機構を付加したことを特徴とする連
続焼成炉。
Claim: What is claimed is: 1. A low temperature zone located near the inlet for evaporating the binder contained in the article to be fired, and a low temperature zone located behind the low temperature zone and passed through the low temperature zone. In a continuous firing furnace provided with a medium temperature zone for preheating a molded body, and a high temperature zone located behind the medium temperature zone for burning the molded body that has passed through the medium temperature zone, from the furnace upper part of the low temperature zone A continuous firing furnace, characterized by adding an exhaust gas removal mechanism for introducing heated air and exhausting it from the hearth.
JP3176493A 1991-07-17 1991-07-17 Continuous baking furnace Pending JPH0526580A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3176493A JPH0526580A (en) 1991-07-17 1991-07-17 Continuous baking furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3176493A JPH0526580A (en) 1991-07-17 1991-07-17 Continuous baking furnace

Publications (1)

Publication Number Publication Date
JPH0526580A true JPH0526580A (en) 1993-02-02

Family

ID=16014631

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3176493A Pending JPH0526580A (en) 1991-07-17 1991-07-17 Continuous baking furnace

Country Status (1)

Country Link
JP (1) JPH0526580A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008249304A (en) * 2007-03-30 2008-10-16 Koyo Thermo System Kk Continuous heat treatment device
JP2013221635A (en) * 2012-04-13 2013-10-28 Tokai Konetsu Kogyo Co Ltd Method and device for treating exhaust gas in baking furnace
JP2015513659A (en) * 2012-03-16 2015-05-14 ゲーカーエン シンター メタルズ ホールディング ゲーエムベーハーGkn Sinter Metals Holding Gmbh Sintering furnace with gas release device
CN109373753A (en) * 2018-12-12 2019-02-22 江苏新江南炉业科技有限公司 A kind of continous way height section rotary drum furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008249304A (en) * 2007-03-30 2008-10-16 Koyo Thermo System Kk Continuous heat treatment device
JP2015513659A (en) * 2012-03-16 2015-05-14 ゲーカーエン シンター メタルズ ホールディング ゲーエムベーハーGkn Sinter Metals Holding Gmbh Sintering furnace with gas release device
JP2013221635A (en) * 2012-04-13 2013-10-28 Tokai Konetsu Kogyo Co Ltd Method and device for treating exhaust gas in baking furnace
CN109373753A (en) * 2018-12-12 2019-02-22 江苏新江南炉业科技有限公司 A kind of continous way height section rotary drum furnace
CN109373753B (en) * 2018-12-12 2024-01-30 江苏新江南炉业科技有限公司 Continuous high-low section roller furnace

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