JPH0684866B2 - Continuous heat treatment furnace - Google Patents

Continuous heat treatment furnace

Info

Publication number
JPH0684866B2
JPH0684866B2 JP2684489A JP2684489A JPH0684866B2 JP H0684866 B2 JPH0684866 B2 JP H0684866B2 JP 2684489 A JP2684489 A JP 2684489A JP 2684489 A JP2684489 A JP 2684489A JP H0684866 B2 JPH0684866 B2 JP H0684866B2
Authority
JP
Japan
Prior art keywords
disk
feeder
area
collector
heater
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
JP2684489A
Other languages
Japanese (ja)
Other versions
JPH02208493A (en
Inventor
逸郎 今津
徹 喜田
健 勝間田
邦彦 中田
真幸 中川
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.)
Tokai Carbon Co Ltd
Original Assignee
Tokai Carbon 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 Tokai Carbon Co Ltd filed Critical Tokai Carbon Co Ltd
Priority to JP2684489A priority Critical patent/JPH0684866B2/en
Publication of JPH02208493A publication Critical patent/JPH02208493A/en
Publication of JPH0684866B2 publication Critical patent/JPH0684866B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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、各種の粉粒体を2000℃を越える高温度域まで
連続的に処理することができる熱処理炉に関する。
TECHNICAL FIELD The present invention relates to a heat treatment furnace capable of continuously treating various powders and granules up to a high temperature range of more than 2000 ° C.

〔従来の技術〕[Conventional technology]

通常、熱処理炉の方式には燃焼により加熱するものと電
気抵抗で発熱するものとがある。また、炉の構造形式と
してはバッチ型のほか各種トンネル炉を用いた連続式の
構造が知られている。
In general, there are two types of heat treatment furnaces: one that heats by combustion and one that generates heat by electric resistance. In addition to the batch type, a continuous type structure using various tunnel furnaces is known as the structural type of the furnace.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

これら従来の熱処理炉のうち、燃焼炉は熱源費用が低廉
で大型受電設備も必要ないという利点がある反面、電気
抵抗炉に比べ騒音、振動、排ガス等による周辺温度の上
昇や環境汚染を惹起し、そのうえ設備スペースの広大
化、自動スタート困難性などの不都合な要素がある。こ
れに対し電気抵抗炉は、高温が比較的簡単に得られる清
浄な炉内環境を整備することができる、騒音、振動、排
ガス等の発生が軽微、温度制御が容易で良好な温度分布
が得られるなど多くの優位性をもつが,熱原価の面では
燃焼炉に及ばない。
Among these conventional heat treatment furnaces, the combustion furnace has the advantages of low heat source cost and no need for large-scale power receiving equipment, but it causes noise, vibration, rise in ambient temperature due to exhaust gas, etc. and environmental pollution compared to the electric resistance furnace. In addition, there are some inconvenient factors such as expansion of equipment space and difficulty of automatic start. On the other hand, the electric resistance furnace can maintain a clean furnace environment in which high temperatures can be obtained relatively easily, noise, vibration, exhaust gas, etc. are minimal, temperature control is easy and good temperature distribution can be obtained. Although it has many advantages, it is inferior to the combustion furnace in terms of heat cost.

また、連続式のトンネル炉には台車炉、プッシャー炉、
ベルコン炉などの方式があるが、台車を用いる場合には
台車が持ち出す熱ロスが大きく、プッシャー炉において
は送り装置およびリターン装置等の複雑な設備を必要と
し、ベルコン炉ではチェーンに使用するセラミック材料
によって炉の使用温度が決まってしまうといった問題点
がある。そのうえ、通常のトンネル炉は完全密閉式でな
いため大気以外のガス雰囲気を必要とする際には多量の
雰囲気ガスを送入しなければならず、排ガスによる熱損
失が無視できない。
For continuous tunnel furnaces, truck furnaces, pusher furnaces,
There is a method such as the Belcon furnace, but when using a dolly, the heat loss brought out by the dolly is large, complicated equipment such as a feeder and a return device is required in the pusher furnace, and the ceramic material used for the chain in the Belcon furnace There is a problem that the operating temperature of the furnace is determined by the above. Moreover, since a normal tunnel furnace is not of a completely closed type, when a gas atmosphere other than the atmosphere is required, a large amount of atmosphere gas must be fed in, and heat loss due to exhaust gas cannot be ignored.

本発明は従来構造による熱処理炉の問題点を解消し、電
気抵抗方式により各種の粉粒体を2000℃を越える高温度
域まで連続的に処理することができる密閉シールタイプ
の熱処理炉を提供するものである。
The present invention solves the problems of the heat treatment furnace having the conventional structure, and provides a hermetically sealed type heat treatment furnace capable of continuously processing various powders by the electric resistance method to a high temperature range exceeding 2000 ° C. It is a thing.

〔課題を解決するための手段〕[Means for Solving the Problems]

すなわち、本発明に係る連続熱処理炉は、断熱材で被包
された密閉内箱の内部に駆動手段により水平回動する回
転デイスクを装備し、該回転デイスクの上面に被処理物
を供給するためのフィーダー、前記フィーダーおよびコ
レクターの対角位置に相当する回転デイスクの上部また
は/および下部に設置された回転デイスク加熱用の棒状
あるいは板状のヒーター、および流入口部が回転デイス
ク面の外縁部にかかる状態にフィーダーと隣接する位置
に設置され、熱処理された被処理物をスクレーパーを介
して回収するためのコレクターを各配設し、回転デイス
ク面においてフィーダーとヒーターまでのデイスク区域
を予熱域、ヒーター発熱部分に相当するデイスク区域を
加熱域、ヒーターからコレクターまでのデイスク区域を
冷却域として区分形成することを構成上の特徴とする。
That is, the continuous heat treatment furnace according to the present invention is equipped with a rotary disk that is horizontally rotated by a driving means inside a closed inner box that is covered with a heat insulating material, and supplies the object to be processed to the upper surface of the rotary disk. Feeder, a rod-shaped or plate-shaped heater for heating the rotating disk installed on the upper and / or lower part of the rotating disk corresponding to the diagonal position of the feeder and the collector, and the inflow port on the outer edge of the rotating disk surface. In such a state, it is installed in a position adjacent to the feeder, each collector is provided for collecting the heat-treated object through the scraper, and the disk area up to the feeder and the heater on the rotating disk surface is preheated and heated. The disk area corresponding to the heat generating part is classified as the heating area, and the disk area from the heater to the collector is classified as the cooling area. It characterized in construction to forming.

密閉内箱は炭素材料のような高温耐熱性の材質で形成
し、その周囲を炭素質粒状体、炭素繊維などの断熱層と
無機質断熱ボードで被包する。その他、密閉内箱の内部
に設置される回転デイスク、フィーダー、スクレーパ
ー、コレクター等の部材も炭素材料で構成することが望
ましい。ヒーターとしては、例えば棒状あるいは板状の
炭素質抵抗発熱体が好適に使用され、フィーダーおよび
コレクターの対角位置に相当する回転デイスクの上部、
下部または上下部にセットする。
The closed inner box is formed of a high temperature heat resistant material such as a carbon material, and the periphery thereof is covered with a heat insulating layer such as carbonaceous granular material and carbon fiber and an inorganic heat insulating board. In addition, it is desirable that members such as a rotary disk, a feeder, a scraper, and a collector installed inside the closed inner box are also made of a carbon material. As the heater, for example, a rod-shaped or plate-shaped carbonaceous resistance heating element is preferably used, and the upper portion of the rotary disk corresponding to the diagonal position of the feeder and the collector,
Set at the bottom or top and bottom.

予熱域、加熱域および冷却域の形成は、フィーダーとヒ
ーター、ヒーターとコレクターの位置間隔が回転デイス
ク面においてそれぞれ略等分となるように設計し、回転
デイスクの回転方向においてフィーダーとヒーターまで
のデイスク区域を予熱域、ヒーター発熱部分に相当する
デイスク区域を加熱域、そしてヒーターからコレクター
までのデイスク区域を冷却域として区分形成する。予熱
域および冷却域には、強制的な予熱手段や冷却手段を設
置する必要はない。
The preheating zone, heating zone, and cooling zone are designed so that the positional distance between the feeder and the heater and the heater and the collector are approximately equal on the rotating disk surface, and the disk between the feeder and the heater is arranged in the rotating direction of the rotating disk. An area is divided into a preheating area, a disk area corresponding to a heater heating portion is a heating area, and a disk area from the heater to the collector is a cooling area. It is not necessary to install compulsory preheating means or cooling means in the preheating zone and the cooling zone.

〔作 用〕[Work]

上記構造の連続熱処理炉において、フィーダーから落下
した被処理物は密閉内箱内を水平回動する回転デイスク
と共に予熱域、加熱域および冷却域を連続して通過し、
最終的にスクレーパーによりコレクターに回収される。
この炉操業を通じて系外への熱の流出は効果的に制御さ
れ、2000℃を越える高温炉内温度を容易に確保すること
ができる。また、密閉シールタイプであるため、多量の
雰囲気ガスを送入する必要はなく、排ガスに伴なう熱損
失の減少、炉体の省スペース化、設備の簡略化等を図る
ことができる。
In the continuous heat treatment furnace having the above structure, the object to be processed dropped from the feeder continuously passes through the preheating zone, the heating zone and the cooling zone together with the rotating disc horizontally rotating in the closed inner box,
Finally, it is collected by the scraper in the collector.
Through this furnace operation, the outflow of heat to the outside of the system is effectively controlled, and it is possible to easily secure a temperature in the high temperature furnace of over 2000 ° C. Further, since it is a hermetically sealed type, it is not necessary to send in a large amount of atmospheric gas, and it is possible to reduce heat loss accompanying exhaust gas, save space in the furnace body, and simplify equipment.

〔実施例〕〔Example〕

以下、本発明の実施例を図面に基づいて説明する。 Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の実施例を示した縦断面図、第2図は第
1図のA−A′線に沿う平断面図、そして第3図の炉の
主要部分を示した斜視説明図である。
1 is a longitudinal sectional view showing an embodiment of the present invention, FIG. 2 is a plan sectional view taken along the line AA 'in FIG. 1, and a perspective explanatory view showing the main part of the furnace in FIG. Is.

これら図において、1は炭素材料で区画形成された密閉
内箱で、その周辺は炭素質粒状断熱材2と外周断熱ボー
ド3で被包されている。密閉内箱1の内部には円周面に
ギヤーが刻設されている炭素材で形成した回転デイスク
4が複数個の底面支持ローラー5および側面支持ローラ
ー6により回動自在に装備されている。7はモーター8
および減速装置9と連結して系外から貫通する駆動軸に
取付けられた炭素製の駆動手段(ピニオン)で、回転デ
イスク4のギヤーと噛合する状態に設置されている。
In these figures, 1 is a closed inner box defined by a carbon material, and the periphery thereof is covered with a carbonaceous granular heat insulating material 2 and a peripheral heat insulating board 3. Inside the closed inner box 1, a rotary disk 4 formed of a carbon material having a gear engraved on its circumferential surface is rotatably mounted by a plurality of bottom surface supporting rollers 5 and side surface supporting rollers 6. 7 is a motor 8
Also, a carbon drive means (pinion) attached to a drive shaft that is connected to the speed reducer 9 and penetrates from the outside of the system is installed so as to mesh with the gear of the rotary disk 4.

10は供給口部11が回転デイスク4の面上に位置する形態
に密閉内箱1の上部から貫通設置されたフィーダー、そ
して12は流入口部13が回転デイスク4面の外縁部にかか
る状態に密閉内箱1の下部に貫通設置されたコレクター
で、前記流入口部13に相当する回転デイスク4の上面に
はスクレーパー14が介設されている。フィーダー10およ
びコレクター12は供給された被処理物が回転デイスク4
上を略一回転して回収されるように隣接して設置し、そ
れぞれにバルグなどの適宜な流量調整装置15、16が付設
されている。
10 is a feeder penetratingly installed from the upper part of the sealed inner box 1 in such a form that the supply port 11 is located on the surface of the rotating disk 4, and 12 is a state in which the inlet 13 is on the outer edge of the surface of the rotating disk 4. The collector is a penetrating installation in the lower part of the closed inner box 1, and a scraper 14 is provided on the upper surface of the rotary disk 4 corresponding to the inflow port 13. The object to be processed supplied to the feeder 10 and the collector 12 is the rotating disk 4
They are installed adjacent to each other so that they can be collected by making a full turn around, and appropriate flow rate adjusting devices 15 and 16 such as a balg are attached to each.

17は棒状の炭素質抵抗発熱体からなる回転デイスク用の
ヒーターで、密閉内箱1における回転デイスク4の上部
または/および下部に複数本設置されている。該ヒータ
ー17はフィーダー10およびコレクター12と対角位置に設
置し、第2図に表示したように回転デイスク4の面上に
予熱域、加熱域および冷却域を区分形成する。
Reference numeral 17 is a heater for a rotating disk, which is composed of a rod-shaped carbonaceous resistance heating element, and a plurality of heaters are installed above and / or below the rotating disk 4 in the sealed inner box 1. The heater 17 is installed at a diagonal position with respect to the feeder 10 and the collector 12, and as shown in FIG. 2, a preheating zone, a heating zone and a cooling zone are formed separately on the surface of the rotary disk 4.

炉運転に際しては、ヒーター17に通電して密閉内箱1の
内部を所定の温度に昇温したのち駆動手段7を作動して
回転デイスク4を水平回動させる。この状態でフィーダ
ー10から粉粒体の被処理物18を供給すると、被処理物18
は回転デイスク4の回動に伴って予熱域、加熱域および
冷却域を連続的に移動し、最終的にスクレーパー14によ
りコレクター12に落下し熱処理を完了する。
During the furnace operation, the heater 17 is energized to raise the temperature of the inside of the closed inner box 1 to a predetermined temperature, and then the driving means 7 is operated to horizontally rotate the rotary disk 4. In this state, when the powdery or granular material 18 is supplied from the feeder 10, the material 18
Moves continuously in the preheating area, the heating area and the cooling area as the rotary disk 4 rotates, and finally falls into the collector 12 by the scraper 14 to complete the heat treatment.

上記構造の本発明による連続熱処理炉を用い、1000℃か
ら2000℃まで10℃/分の昇温速度で上昇し、2000℃に30
分間保持したのち2000℃から1000℃まで10℃/分の速度
で昇温させる温度条件により平均直径2mmの炭素球状体
を熱処理したところ、処理量1kgに要した電力は12KW
で、N2ガス送入量60/kg時の被処理物の酸化消耗量は
0.2%であった。
Using the continuous heat treatment furnace of the present invention having the above structure, the temperature was raised from 1000 ° C. to 2000 ° C. at a heating rate of 10 ° C./min, and the temperature was increased to 30 ° C. at 2000 ° C.
After holding for a minute, heat treatment was performed on carbon spheres with an average diameter of 2 mm under the temperature conditions of heating from 2000 ° C to 1000 ° C at a rate of 10 ° C / min.
And, the amount of oxidative consumption of the processed material when the N 2 gas feed rate is 60 / kg is
It was 0.2%.

比較のために、従来構造のプッシャー式トンネル炉を用
い、常温から2000℃まで10℃/分の昇温速度で上昇し、
2000℃に30分間保持したのち2000℃から常温まで10℃/
分で降温させる温度条件により同一の炭素球状体を熱処
理した。この場合の電力量は60KW/kgで、N2ガス送入量1
000/kg時の酸化消耗量は1.5%であった。
For comparison, using a pusher type tunnel furnace with a conventional structure, the temperature was raised from room temperature to 2000 ° C. at a heating rate of 10 ° C./min,
After holding at 2000 ℃ for 30 minutes, from 2000 ℃ to room temperature 10 ℃ /
The same carbon spheres were heat-treated under the temperature condition of lowering the temperature in minutes. The electric power in this case is 60 KW / kg, and the N 2 gas feed rate is 1
The oxidative consumption at 000 / kg was 1.5%.

〔発明の効果〕〔The invention's effect〕

以上のとおり、本発明よれば優れた熱効率により容易に
2000℃を越える高温が確保できるコンパクトかつ簡易構
造の連続熱処理炉が提供されるから、各種粉粒体の熱処
理を能率よく遂行することができる。
As described above, according to the present invention, excellent thermal efficiency facilitates
Since a compact and simple structure continuous heat treatment furnace capable of ensuring a high temperature exceeding 2000 ° C. is provided, heat treatment of various powders can be efficiently performed.

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

第1図は本発明の実施例を示した縦断面図、第2図は第
1図のA−A′線に沿う平断面図である。第3図は、本
発明炉の主要部分を示した斜視説明図である。 1……密閉内箱、2……炭素質粒状断熱材、 3……外周断熱ボード、4……回転デイスク、 5……底面支持ローラー、 6……側面支持ローラー、7……駆動手段、 8……モーター、9……減速装置、 10……フィーダー、11……供給口部、 12……コレクター、13……流入口部、 14……スクレーパー、 15、16……流量調整装置、 17……ヒーター、18……被処理物。
1 is a vertical sectional view showing an embodiment of the present invention, and FIG. 2 is a plane sectional view taken along the line AA 'in FIG. FIG. 3 is a perspective explanatory view showing a main part of the furnace of the present invention. 1 ... Closed inner box, 2 ... Carbonaceous granular heat insulating material, 3 ... Peripheral heat insulating board, 4 ... Rotating disk, 5 ... Bottom supporting roller, 6 ... Side supporting roller, 7 ... Driving means, 8 ...... Motor, 9 ...... Reduction device, 10 …… Feeder, 11 …… Supply port, 12 …… Collector, 13 …… Inlet port, 14 …… Scraper, 15, 16 …… Flow adjustment device, 17 ・ ・ ・… Heater, 18… Object to be processed.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】断熱材(2)で被包された密閉内箱(1)
の内部に駆動手段(7)により水平回動する回転デイス
ク(4)を装備し、該回転デイスクの上面に被処理物を
供給するためのフィーダー(10)、前記フィーダー(1
0)およびコレクター(12)の対角位置に相当する回転
デイスクの上または/および下に設置された回転デイス
ク加熱用の棒状あるいは板状のヒーター(17)、および
流入口部(13)が回転デイスク面の外縁部にかかる状態
にフィーダー(10)と隣接する位置に設置され、熱処理
された被処理物をスクレーパー(14)を介して回収する
ためのコレクター(12)を各配設し、回転デイスク面に
おいてフィーダー(10)とヒーター(17)までのデイス
ク区域を予熱域、ヒーター発熱部分に相当するデイスク
区域を加熱域、ヒーター(17)からコレクター(12)ま
でのデイスク区域を冷却域として区分形成してなること
を特徴とする連続熱処理炉。
1. A closed inner box (1) covered with a heat insulating material (2).
A rotary disk (4) that is horizontally rotated by a driving means (7) is provided inside the feeder, and a feeder (10) for supplying an object to be processed onto the upper surface of the rotary disk, the feeder (1).
0) and the collector (12) diagonally located on the rotary disk, which is installed above and / or below the rotary disk for heating the rotary disk, such as a rod-shaped or plate-shaped heater (17) and the inlet (13) rotate The collector (12) is installed at a position adjacent to the feeder (10) so as to cover the outer edge of the disk surface, and each collector (12) for collecting the heat-treated object through the scraper (14) is arranged and rotated. On the disk surface, the disk area from the feeder (10) and the heater (17) is classified as the preheating area, the disk area corresponding to the heater heat generation area is classified as the heating area, and the disk area from the heater (17) to the collector (12) is classified as the cooling area. A continuous heat treatment furnace characterized by being formed.
JP2684489A 1989-02-06 1989-02-06 Continuous heat treatment furnace Expired - Lifetime JPH0684866B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2684489A JPH0684866B2 (en) 1989-02-06 1989-02-06 Continuous heat treatment furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2684489A JPH0684866B2 (en) 1989-02-06 1989-02-06 Continuous heat treatment furnace

Publications (2)

Publication Number Publication Date
JPH02208493A JPH02208493A (en) 1990-08-20
JPH0684866B2 true JPH0684866B2 (en) 1994-10-26

Family

ID=12204584

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2684489A Expired - Lifetime JPH0684866B2 (en) 1989-02-06 1989-02-06 Continuous heat treatment furnace

Country Status (1)

Country Link
JP (1) JPH0684866B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109444210A (en) * 2018-12-19 2019-03-08 宝钛集团有限公司 A kind of dedicated sample heat-treatment furnace of transformation temperature test

Also Published As

Publication number Publication date
JPH02208493A (en) 1990-08-20

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