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JPH0612709B2 - Atmosphere control device for induction heating furnace - Google Patents
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JPH0612709B2 - Atmosphere control device for induction heating furnace - Google Patents

Atmosphere control device for induction heating furnace

Info

Publication number
JPH0612709B2
JPH0612709B2 JP59156770A JP15677084A JPH0612709B2 JP H0612709 B2 JPH0612709 B2 JP H0612709B2 JP 59156770 A JP59156770 A JP 59156770A JP 15677084 A JP15677084 A JP 15677084A JP H0612709 B2 JPH0612709 B2 JP H0612709B2
Authority
JP
Japan
Prior art keywords
furnace
gas
induction heating
steel material
oxygen 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
JP59156770A
Other languages
Japanese (ja)
Other versions
JPS6134883A (en
Inventor
正満 小橋
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP59156770A priority Critical patent/JPH0612709B2/en
Publication of JPS6134883A publication Critical patent/JPS6134883A/en
Publication of JPH0612709B2 publication Critical patent/JPH0612709B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

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  • General Induction Heating (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は,圧延またはプレス等の加工を熱間で実施する
工程において,鋼材を急速にかつ短時間のうちに所定の
高温度に加熱する誘導加熱炉に関するもので,さらに詳
言すれば,誘導加熱炉内における鋼材表面スケールの発
生および溶融等を効果的に防止することを目的としたも
のである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention rapidly heats a steel material to a predetermined high temperature in a short time in a process of hot working such as rolling or pressing. The present invention relates to an induction heating furnace, and more specifically, it is intended to effectively prevent generation and melting of steel material surface scale in the induction heating furnace.

〔従来の技術〕[Conventional technology]

鋼材を短時間の内に所定の高温度まで急速加熱する誘導
加熱炉において,炉内雰囲気の酸素ガス含有量および鋼
材加熱時の表面温度による酸化量が変化する様子を第5
図に示す。
In an induction heating furnace that rapidly heats steel to a predetermined high temperature within a short period of time, the state that the oxygen gas content of the furnace atmosphere and the amount of oxidation due to the surface temperature during steel heating change
Shown in the figure.

この第5図において,曲線a4は炉内酸素ガス濃度が20%
の場合の変化特性を,曲線a5は炉内酸素ガス濃度が1%
の場合の変化特性を,そして曲線a6は炉内酸素ガス濃度
が0.1%以下の場合の変化特性をそれぞれ示している。
In Fig. 5, the curve a4 shows that the oxygen gas concentration in the furnace is 20%.
Curve a5 shows that the oxygen gas concentration in the furnace is 1%
And the curve a6 shows the change characteristics when the oxygen gas concentration in the furnace is 0.1% or less.

この第5図から明らかなように,鋼材を少なくとも1250
℃以上に加熱する場合,炉内酸素ガス濃度を低下させる
ことにより,鋼材の酸化減量を著しく減らすことがで
き,これによって歩留り向上およびスケール発生に起因
する製品表面欠陥を大幅に防止することが可能となる。
As is clear from Fig. 5, at least 1250 steel is used.
When heating above ℃, by reducing the oxygen gas concentration in the furnace, it is possible to significantly reduce the oxidation loss of the steel material, which can greatly improve the yield and prevent product surface defects due to scale generation. Becomes

また,鋼材の表面に酸化物であるスケールが発生する
と,この酸化物であるスケールはその融点が低く,1300
℃程度で溶融するので,この溶融したスケールは誘導加
熱炉の操業性を損なうばかりでなく,鋼材の表面欠陥,
耳割れ発生等の多くの問題を生じる不都合があった。
In addition, when scale that is an oxide is generated on the surface of the steel material, the scale that is this oxide has a low melting point and
Since it melts at about ℃, this molten scale not only impairs the operability of the induction heating furnace, but also causes surface defects in the steel.
There is an inconvenience that causes many problems such as ear cracking.

それゆえ,誘導加熱炉の炉内雰囲気の制御,すなわち炉
内の酸素ガス濃度の制御は重要な意味を持ち,不活性ガ
ス等の雰囲気ガスを炉内に封入して鋼材表面の酸化を防
止する対策が提案され,いくつかの手段が報告されてい
る。
Therefore, the control of the atmosphere in the induction heating furnace, that is, the control of the oxygen gas concentration in the furnace, has an important meaning, and an atmosphere gas such as an inert gas is enclosed in the furnace to prevent the oxidation of the steel surface. Countermeasures have been proposed and some measures have been reported.

例えば,実公昭58−24397号公報,実開昭48−
113741号公報さらには実開昭48−91555号
公報等があるが,これらの従来技術に示された手段は,
不活性ガスの炉内への送入方法であり,また炉下部のシ
ール構造に関するものであるが,基本的には,炉外から
不活性ガスを炉内に送入し,炉内雰囲気を或る設定され
たレベルに維持するものとなっている。
For example, Japanese Utility Model Publication No. 58-24397, Japanese Utility Model Publication No. 48-
Japanese Patent No. 113741 and Japanese Utility Model Laid-Open No. 48-91555 disclose the means disclosed in these prior arts.
This is a method of feeding an inert gas into the furnace, and relates to a sealing structure at the lower part of the furnace. Basically, the inert gas is fed into the furnace from the outside of the furnace to control the atmosphere inside the furnace. It is supposed to be maintained at the set level.

〔発明が解消しようとする問題点〕[Problems to be solved by the invention]

しかしながら,これらの上記した従来の手段では,次の
ような不都合な問題がある。
However, these conventional means described above have the following inconvenient problems.

すなわち,炉内への鋼材の装入,注出時においては,炉
を開放する必要があるので,炉内への外気の侵入を阻止
することができず,炉内の雰囲気は,炉の開閉操作の度
にそのかなりの量が外気と置換されてしまう,すなわち
炉の開閉操作の度に大量の酸素ガスが外部から炉内に侵
入することになる。
That is, since it is necessary to open the furnace at the time of charging and discharging the steel material into the furnace, it is not possible to prevent the outside air from entering the furnace, and the atmosphere in the furnace changes the opening and closing of the furnace. A large amount of it is replaced with the outside air at every operation, that is, a large amount of oxygen gas intrudes into the furnace from the outside every time the furnace is opened and closed.

この大量の酸素ガスを炉内に侵入させたまま炉内に不活
性ガスを送入し,もって炉内の酸素ガス濃度を低下させ
るには,極めて大量の不活性ガスを必要とすることにな
る。
An extremely large amount of inert gas is required in order to feed the inert gas into the furnace while allowing the large amount of oxygen gas to enter the furnace and thereby reduce the oxygen gas concentration in the furnace. .

ちなみに,炉内の初期の酸素ガス濃度を10%とし,こ
の酸素ガス濃度を低下させるのに必要な送入不活性ガス
の量は,実験の結果によると第6図のようになる。
Incidentally, the initial oxygen gas concentration in the furnace is set to 10%, and the amount of inert gas fed in to reduce the oxygen gas concentration is as shown in Fig. 6 according to the experimental results.

すなわち,この第6図の曲線a7から明らかなように,炉
内の酸素ガス濃度を初期酸素ガス濃度の5%とするため
には,炉内空間の約5倍の容量の不活性ガスが必要とな
るのである。
That is, as is clear from the curve a7 in Fig. 6, in order to set the oxygen gas concentration in the furnace to 5% of the initial oxygen gas concentration, an inert gas of about 5 times the volume in the furnace space is required. It becomes.

また,誘導加熱炉の特徴は,鋼材を短時間の内の所定の
高温度まで急速加熱することにあるのであるから,炉内
雰囲気の調整は当然のこととして短時間の内に達成され
なければならず,もしこの炉内雰囲気の調整に長時間を
要するようでは,炉の生産性を確保することは不可能と
なる。
Further, since the characteristic of the induction heating furnace is that the steel material is rapidly heated to a predetermined high temperature within a short time, the atmosphere inside the furnace must be adjusted within a short time as a matter of course. However, if it takes a long time to adjust the atmosphere in the furnace, it becomes impossible to secure the productivity of the furnace.

このようなことから,短時間の内に,鋼材の装入,抽出
を繰り返す誘導加熱炉においては,不活性ガスの炉内へ
の押し込みだけによる炉内雰囲気の置換だけでは,炉内
雰囲気調整の速度に限界のあることが明らかである。
Therefore, in an induction heating furnace in which charging and extraction of steel materials are repeated within a short time, it is possible to adjust the atmosphere in the furnace by only replacing the atmosphere in the furnace by pushing the inert gas into the furnace. It is clear that there is a speed limit.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は,上記した従来例における問題点を解消すべく
創案されたもので,誘導加熱炉により鋼材を急速加熱す
るに際し,有効な炉内雰囲気制御を達成するために,炉
内ガスの吸引操作と不活性ガスを使用した雰囲気ガスの
炉内への押し込み操作とを組合わせるべく構成したもの
で,以下本発明を,本発明の一実施例を示す図面を参照
しながら説明する。
The present invention was devised to solve the above-mentioned problems in the conventional example, and when a steel material is rapidly heated by an induction heating furnace, in order to achieve effective furnace atmosphere control, a furnace gas suction operation is performed. The present invention will be described below with reference to the drawings showing an embodiment of the present invention.

本発明による誘導加熱炉の炉内雰囲気制御装置は,鋼材
15を雰囲気ガス中で再加熱する誘導加熱炉の炉体1内に
加熱鋼材15を挿入しそして密閉した後に炉内ガスを吸引
・排出する吸引装置12と,この吸引装置12による炉内ガ
ス吸引排出操作後に不活性ガスを使用した雰囲気ガスを
炉体1内に供給するガス供給装置8と,炉体1内の酸素
ガス濃度を分析検出する分析計6と,この分析計6の分
析結果信号S1に従って炉体1内の酸素ガス濃度を予め設
定された一定値以下にすべく前記ガス供給装置8の炉体
1内に対する雰囲気ガス供給量を制御する制御器7とを
具備して構成されている。
A furnace atmosphere control device for an induction heating furnace according to the present invention is a steel material.
Suction device 12 that sucks and discharges the furnace gas after inserting and sealing the heated steel material 15 into the furnace body 1 of the induction heating furnace that reheats 15 in the atmospheric gas, and the furnace gas suction by this suction device 12 A gas supply device 8 for supplying an atmosphere gas using an inert gas into the furnace body 1 after the discharging operation, an analyzer 6 for analyzing and detecting the oxygen gas concentration in the furnace body 1, and an analysis result signal of the analyzer 6. A controller 7 for controlling the amount of atmospheric gas supplied to the inside of the furnace body 1 of the gas supply device 8 in order to keep the oxygen gas concentration in the furnace body 1 below a predetermined constant value according to S1. There is.

分析計6は,炉体1内のガスを常時サンプリング採取し
て,この採取したガス中の酸素ガスの濃度を分析検出し
ており,この酸素ガスの濃度の検出値は,信号S1として
常時制御器7に出力されている。
The analyzer 6 constantly samples the gas in the furnace body 1 and analyzes and detects the concentration of oxygen gas in the collected gas. The detected value of the concentration of oxygen gas is constantly controlled as a signal S1. It is output to the container 7.

制御器7はマイクロコンピュータ等により構成されたも
ので,分析計6からの信号S1に従って,ガス供給装置8
の炉体1内への雰囲気ガスの供給量を制御するものとな
っている。
The controller 7 is composed of a microcomputer or the like, and according to the signal S1 from the analyzer 6, the gas supply device 8
The supply amount of the atmospheric gas into the furnace body 1 is controlled.

〔作用〕[Action]

本発明による炉内雰囲気制御装置は,上記の如き構成と
なっているものであるが,次にこの本発明装置の基本的
作用を順に説明する。
The in-furnace atmosphere control device according to the present invention is configured as described above. Next, the basic operation of the present invention device will be described in order.

分析計6は,炉体1に開口形成された採取口5から炉内
ガスをサンプリング採取して炉内ガス中の酸素ガス濃度
を連続して分析検出して,この検出信号S1を制御器7に
出力している。
The analyzer 6 samples the furnace gas from the sampling port 5 formed in the furnace body 1, continuously analyzes and detects the oxygen gas concentration in the furnace gas, and outputs the detection signal S1 to the controller 7 Is output to.

この状態から,鋼材15を積載したスキッド部3が上昇し
て鋼材15を炉体1内に装入すると同時に炉体1を密閉す
る。
From this state, the skid portion 3 loaded with the steel material 15 rises to load the steel material 15 into the furnace body 1 and at the same time seal the furnace body 1.

炉体1の密閉が達成されると加熱コイル2に電流が供給
されて鋼材15の誘導加熱動作が開始されるが,この誘導
加熱炉の加熱動作の開始と同時に制御器7に制御開始信
号S2が出力される。
When the sealing of the furnace body 1 is achieved, a current is supplied to the heating coil 2 to start the induction heating operation of the steel material 15. At the same time when the heating operation of the induction heating furnace is started, the control start signal S2 is sent to the controller 7. Is output.

すなわち,扉閉信号により制御器7に制御開始信号S2を
出力するのである。
That is, the control start signal S2 is output to the controller 7 by the door closing signal.

この制御開始信号S2の入力により制御器7は信号S1に従
った制御信号S3をガス供給装置8および吸引装置12に出
力する。
When the control start signal S2 is input, the controller 7 outputs the control signal S3 according to the signal S1 to the gas supply device 8 and the suction device 12.

制御器7からの制御信号S3の入力よって,まずガス供給
装置8は雰囲気ガスの炉体1内への供給路を遮断するの
に対し,吸引装置12が作動して炉体1内のガスを吸引排
出する。
Due to the input of the control signal S3 from the controller 7, the gas supply device 8 first shuts off the supply path of the atmospheric gas into the furnace body 1, while the suction device 12 operates to remove the gas in the furnace body 1. Aspirate and discharge.

この吸引装置12の所望時間の作動後,吸引装置12を停止
させると同時にガス供給装置8を作動させて,炉体1内
に雰囲気ガスを送入して炉体1内を復圧し,以後分析計
6による分析値,すなわち酸素ガス濃度が予め設定され
た目標濃度以下となるように制御信号S3によってガス供
給装置8から炉体1内への雰囲気ガスの投入量をコント
ロールし,もって一定酸素ガス濃度以下での鋼材15の誘
導加熱操作を達成する。
After the suction device 12 has been operated for a desired time, the suction device 12 is stopped, and at the same time, the gas supply device 8 is operated to feed an atmospheric gas into the furnace body 1 to restore the pressure inside the furnace body 1 and then analyze it. The input value of the atmospheric gas from the gas supply device 8 into the furnace body 1 is controlled by the control signal S3 so that the analysis value by the total 6, that is, the oxygen gas concentration becomes equal to or less than the preset target concentration, and thus the constant oxygen gas is maintained. The induction heating operation of the steel material 15 below the concentration is achieved.

〔実施例〕〔Example〕

第1図図示実施例の場合,炉体1の側壁に,炉内ガスの
吸引および炉体1内への雰囲気ガスの投入を行うための
吸引・投入口4が開口されていると共に,炉体1の頂壁
に炉体ガスの採取口5が開口形成されている。
In the case of the embodiment shown in FIG. 1, the side wall of the furnace body 1 is provided with a suction / charge port 4 for sucking the gas inside the furnace and for charging the atmospheric gas into the furnace body 1, and A furnace body gas sampling port 5 is formed on the top wall of the opening 1.

採取口5を炉体1の頂壁に形成したのは,炉内温度が炉
外温度よりもかなり高いレベルにあることから,炉内ガ
スがドラフト効果により,炉内において上昇方向の流れ
となることから,炉内上部の雰囲気の方が代表性がある
と考えられるからである。
The sampling port 5 is formed on the top wall of the furnace body 1 because the temperature inside the furnace is at a level considerably higher than the temperature outside the furnace, and therefore the gas inside the furnace flows upward in the furnace due to the draft effect. Therefore, it is considered that the atmosphere in the upper part of the furnace is more representative.

ただし,これは一般的に言えることであって,設備の特
殊性により,任意に決定しても差支えないことは云うま
でもない。
However, this is generally true, and it goes without saying that it can be arbitrarily determined depending on the peculiarities of the equipment.

採取口5から採取された炉内ガスは,分析計6に導入さ
れ,炉内ガス中の成分を分析把握する。
The in-furnace gas sampled from the sampling port 5 is introduced into the analyzer 6 to analyze and grasp the components in the in-furnace gas.

本発明装置の目的は,炉体1内をできる限り非酸化状態
とすることにあるから,炉内酸素ガス濃度をコントロー
ルする必要があり,それゆえ分析計6としては一般的な
酸素ガス連続分析計(例えば,ジルコニア式)が最適で
ある。
Since the purpose of the device of the present invention is to make the inside of the furnace body 1 as non-oxidized as possible, it is necessary to control the oxygen gas concentration in the furnace. A total (eg, zirconia type) is optimal.

炉内酸素ガス濃度の管理目標値としては,第5図に示し
た酸化減量特性から,1250℃以上の加熱に対して酸素ガ
ス濃度が1%以下となるのが望ましい。
From the oxidation weight loss characteristics shown in Fig. 5, it is desirable that the oxygen gas concentration be 1% or less for heating above 1250 ° C, as the control target value of the oxygen gas concentration in the furnace.

この分析計6による酸素ガス濃度の分析・検出値は信号
S1として制御器7に入力される。
The analysis / detection value of oxygen gas concentration by this analyzer 6 is a signal
It is input to the controller 7 as S1.

吸入・投入口4に対してはガス供給装置8と吸入装置12
とが並列に接続されており,ガス供給装置8は雰囲気ガ
スである不活性ガス源9と流量調節弁10とそして流量計
11とから構成されており,吸引装置12は真空ポンプ13と
切換弁14とから構成されている。
A gas supply device 8 and a suction device 12 for the suction / input port 4
Are connected in parallel, and the gas supply device 8 includes an inert gas source 9 as an atmospheric gas, a flow rate control valve 10, and a flow meter.
11 and the suction device 12 is composed of a vacuum pump 13 and a switching valve 14.

この第1図図示実施例は,次の如き順序で操作される。The embodiment shown in FIG. 1 is operated in the following order.

まず,鋼材15をスキッド部3に積載して上昇させ,もっ
て鋼材15を炉体1内に装入する。
First, the steel material 15 is loaded on the skid portion 3 and lifted up, so that the steel material 15 is loaded into the furnace body 1.

次いで,下部扉(図示省略)を上昇位置で停止させると
扉閉信号が発信され,流量調節弁10を閉状態にすると共
に切換弁14を開状態とし,さらに真空ポンプ13を起動す
る。
Next, when the lower door (not shown) is stopped at the raised position, a door closing signal is transmitted, the flow rate control valve 10 is closed, the switching valve 14 is opened, and the vacuum pump 13 is started.

この扉開信号は,直接流量調節弁10,切換弁14そして真
空ポンプ13に入力されるようにしても良いのであるが,
第1図図示実施例の場合,制御器7に対して始動指令信
号S2として入力され,制御器7はこの信号S2の入力に従
って,制御信号S3を流量調節弁10,切換弁14そして真空
ポンプ13に出力する。
The door open signal may be directly input to the flow rate control valve 10, the switching valve 14 and the vacuum pump 13.
In the case of the embodiment shown in FIG. 1, a start command signal S2 is input to the controller 7, and the controller 7 sends the control signal S3 according to the input of this signal S2 to the flow control valve 10, the switching valve 14 and the vacuum pump 13. Output to.

この制御信号S3は,指令信号S2の入力に従って発信され
た当初においては,流量調節弁10に対しては“閉”信号
として出力され,切換弁14に対しては“閉”信号として
出力され,そして真空ポンプ13に対して起動信号として
出力される。
This control signal S3 is output as a "closed" signal to the flow rate control valve 10 and is output as a "closed" signal to the switching valve 14 at the beginning when it is transmitted according to the input of the command signal S2. Then, it is output to the vacuum pump 13 as a start signal.

真空ポンプ13による炉内ガスの吸引・排出が進んで分析
計6による酸素ガス濃度の分析値が,予め設定した目標
値以下となりかつ誘導加熱炉が定常操業に入った段階
で,制御器7からの信号S3により,真空ポンプ13を停止
させると共に切換弁14を“閉”状態とし,さらに流量調
節弁10を全開状態とする。
When the suction / discharge of the gas in the furnace by the vacuum pump 13 progresses and the analysis value of the oxygen gas concentration by the analyzer 6 becomes less than or equal to the preset target value and the induction heating furnace enters the steady operation, the controller 7 Signal S3, the vacuum pump 13 is stopped, the switching valve 14 is closed, and the flow rate control valve 10 is fully opened.

この流量調節弁10の全開によって不活性ガス源9から炉
体1内に窒素ガス等の雰囲気ガスが一気に供給されて,
炉体1内を復圧させると共に,炉体1内の復圧後は分析
計6による分析値が予め設定された目標値となるよう流
量調節弁10の開度を調節して不活性ガス源9から炉体1
内への雰囲気ガスの投入量をコントロールする。
When the flow rate control valve 10 is fully opened, an inert gas source 9 supplies atmospheric gas such as nitrogen gas into the furnace body 1 at a stroke,
The pressure inside the furnace body 1 is restored, and after the pressure inside the furnace body 1 is restored, the opening of the flow control valve 10 is adjusted so that the analysis value by the analyzer 6 becomes a preset target value. 9 to furnace body 1
Control the amount of atmospheric gas input into the inside.

なお,切換弁14の開閉を制御器7からの信号S3によって
行う場合を説明したが,この切換弁14の開閉および真空
ポンプ13の起動・停止制御は,炉体1内部容積が一定で
あることから,タイマーにより扉閉信号の発信時点を起
点として制御するようにすることも可能である。
The case where the switching valve 14 is opened / closed by the signal S3 from the controller 7 has been described. However, the opening / closing of the switching valve 14 and the start / stop control of the vacuum pump 13 require that the internal volume of the furnace body 1 be constant. Therefore, it is possible to control with the timer starting from the point of time when the door closing signal is transmitted.

所で,上記した一連の制御動作中において,適当な一定
時間の間,炉内ガスを吸引し続けても,炉内ガス中の酸
素ガス濃度が低下しないか,あるいは或る量以上の雰囲
気ガスを炉体1内に投入しても,炉内ガスの酸素ガス濃
度が低下しないような場合には,誘導加熱炉のシール性
に重大な問題が発生していると考えられるので,警報あ
るいはCRT表示等によりオペレータに知らせることが
でき,根本的な対策を早期に実施することが可能とな
る。
However, during the above-mentioned series of control operations, even if the in-furnace gas is continuously sucked for an appropriate fixed time, the oxygen gas concentration in the in-furnace gas does not decrease or a certain amount of atmospheric gas or more If the oxygen gas concentration in the furnace gas does not decrease even after the gas is charged into the furnace body 1, it is considered that a serious problem has occurred in the sealing performance of the induction heating furnace. The operator can be notified by means of a display, etc., and fundamental measures can be implemented early.

次に,一つの実施結果例を示す。Next, an example of one implementation result is shown.

第2図に示す如く,炉体1の炉内寸法は,長さR1が1250
0mm,また幅R3が450mm,そして高さR2が1800mmで,この
炉体1内に装入・加熱される鋼材15の寸法は,長さK1が
12200mm,幅K3が215mmそして高さK2が1300mmである。
As shown in Fig. 2, the internal dimensions of the furnace body 1 are that the length R1 is 1250.
With a width R3 of 450 mm and a height R2 of 1800 mm, the dimensions of the steel material 15 charged and heated in the furnace body 1 are that the length K1 is
It measures 12200 mm, width K3 is 215 mm, and height K2 is 1300 mm.

それゆえ,鋼材15の体積を除いた炉体1内の容積は6.7m
3となる。
Therefore, the volume inside the furnace body 1 excluding the volume of the steel material 15 is 6.7 m.
It becomes 3 .

また,鋼材15に対する加熱パターンは,30分加熱,5
分均熱であり,鋼材15の表面温度変化特性曲線a1は,第
3図に示す如き形態となる。
The heating pattern for steel material 15 is 30 minutes heating, 5
The temperature distribution characteristic curve a1 of the steel material 15 has a form as shown in FIG.

なお,鋼材15は,誘導加熱炉の電力原単位の削減等を目
的にホットチャージされており,また鋼材15の表面温度
は炉体1の炉壁に取付けた放射温度計によって常時連続
して測温されている。
The steel material 15 is hot-charged for the purpose of reducing the electric power consumption of the induction heating furnace, and the surface temperature of the steel material 15 is continuously measured by the radiation thermometer attached to the furnace wall of the furnace body 1. It is warm.

この具体例では,鋼材15の加熱温度が,鋼材15の表面で
1300℃と高いので,第5図から明らかなように,酸化減
量を充分に小さい値に抑えるために,炉内ガス中の酸素
ガス濃度を1%以下に制御管理する必要がある。
In this specific example, the heating temperature of the steel material 15 is
Since it is as high as 1300 ° C, as is clear from Fig. 5, it is necessary to control and control the oxygen gas concentration in the furnace gas to 1% or less in order to suppress the oxidation loss to a sufficiently small value.

鋼材15の加熱開始時(第3図において装入完時であり,
第4図においてはt1時である)には,下部扉開による炉
体1内への外気の侵入で炉内の酸素ガス濃度が高くなっ
ている。
At the start of heating the steel material 15 (when charging is completed in Fig. 3,
At time t1 in FIG. 4), the oxygen gas concentration in the furnace becomes high due to the invasion of outside air into the furnace body 1 by opening the lower door.

本具体例では,約5分の炉内ガス吸引時間(第4図にお
いて,時点t1から時点t2までの間)で炉内ガス中におけ
る酸素ガス濃度を1%以下にしている。
In this specific example, the oxygen gas concentration in the furnace gas is set to 1% or less during the furnace gas suction time of about 5 minutes (from time t1 to time t2 in FIG. 4).

第3図に示した鋼材表面温度変化曲線a1から明らかな如
く,加熱開始後5分では,鋼材15の表面温度は1100℃程
度であるので,これ以上早く炉内ガスを吸引して酸素ガ
ス濃度を早く下げる必要が少ないことから,上記した吸
引速度時間程度に設定している。
As is clear from the steel material surface temperature change curve a1 shown in Fig. 3, the surface temperature of the steel material 15 is about 1100 ° C 5 minutes after the start of heating. Since it is not necessary to lower the suction speed quickly, the suction speed is set to the above-mentioned time.

第4図から明らかなように,炉内ガス吸引完了後(時点
t2後),炉内圧を大気圧+α(αは+1mmH2O程度)の
正圧に復圧させる必要から雰囲気ガスである窒素ガスが
大量にかつ急速に炉内に投入されている。
As is clear from Fig. 4, after completion of the gas suction in the furnace (time point
After t2), a large amount of nitrogen gas, which is the atmospheric gas, is rapidly injected into the furnace because it is necessary to restore the internal pressure to the positive pressure of atmospheric pressure + α (α is about +1 mmH 2 O).

炉内の復圧が達成された時点t3以後は,炉内ガス中の酸
素ガスの分析値に従って雰囲気ガスの炉内への投入量制
御が始まり,定常操業となっている。
After the time t3 when the recompression in the furnace is achieved, the control of the amount of the atmospheric gas introduced into the furnace is started according to the analysis value of the oxygen gas in the furnace gas, and the operation is steady.

また,鋼材15の表面温度が1250℃以上の酸化し易い高温
域において,炉内ガス中の酸素ガス濃度が0.5〜1%の
範囲内にコントロールされていることが酸素ガス濃度曲
線a3が明確に示している。
In addition, the oxygen gas concentration curve a3 clearly shows that the oxygen gas concentration in the furnace gas is controlled within the range of 0.5 to 1% in the high temperature region where the surface temperature of the steel material 15 is easily oxidized at 1250 ° C or higher. Shows.

〔発明の効果〕〔The invention's effect〕

以上の説明から明らかな如く,本発明による誘導加熱炉
の炉内雰囲気制御装置は,極めて短時間の内に炉内ガス
中の酸素ガス濃度を充分に低い目標値以下に低下させる
ことができるので,誘導加熱炉の特徴である短時間の内
の鋼材の急速加熱を充分に生かすことができ,これによ
って炉の高い生産性を確保することができる。
As is clear from the above description, the furnace atmosphere control device for an induction heating furnace according to the present invention can reduce the oxygen gas concentration in the furnace gas to a sufficiently low target value or less within an extremely short time. The rapid heating of steel material within a short time, which is a characteristic of the induction heating furnace, can be fully utilized, and thus high productivity of the furnace can be secured.

また,炉内ガス中における酸素ガス濃度を目標値以下に
するのに消費される雰囲気ガスの量を従来の場合に比べ
て遥かに少なくすることができ,これによって雰囲気ガ
スの消費量を少なくすることができると共に,雰囲気ガ
スに関する設備を小型・簡単化することができることに
よる経済的効果が高い。
In addition, the amount of atmospheric gas consumed to bring the oxygen gas concentration in the furnace gas below the target value can be made much smaller than in the conventional case, thereby reducing the amount of atmospheric gas consumed. In addition, it is possible to reduce the size and simplification of the equipment related to the atmosphere gas, which is highly economical.

さらに,炉内ガスの吸引・排出による炉内ガス中の酸素
ガス濃度の低下程度は,ほぼ一定した特性となることが
予め知られているので,この酸素ガス濃度の低下速度を
監視することによって,炉の気密性の不良を早期にかつ
確実に検出することができ,これによって良好な鋼材加
熱を達成することができる等,ようするに短時間に炉内
のガス置換が可能であり,置換するに必要な投入ガス量
を低減可能であり,押し込みガス置換では炉内が冷却さ
れて炉の加熱効率が低下するが押し込みガス量の少ない
本発明装置においては炉効率の向上を計ることができる
等多くの優れた効果を発揮するものとなっている。
Furthermore, it is known in advance that the degree of decrease in the oxygen gas concentration in the furnace gas due to the suction and discharge of the furnace gas has a substantially constant characteristic. The gas tightness of the furnace can be detected early and surely, and thereby good steel heating can be achieved. Therefore, it is possible to replace the gas in the furnace in a short time. It is possible to reduce the required amount of input gas, and the inside of the furnace is cooled by pushing gas replacement and the heating efficiency of the furnace is reduced, but in the device of the present invention with a small amount of pushing gas, it is possible to improve the furnace efficiency It is the one that exhibits the excellent effect of.

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

第1図は,本発明装置の構成の一実施例を示す説明図で
ある。 第2図は,本発明装置の機能を実施するための具体例を
示す炉体の斜視図である。 第3図は,誘導加熱炉による鋼材表面温度の特性を示す
線図である。 第4図は,本発明装置による制御動作の一例を示す不活
性ガスの炉体内への供給量変化曲線図および炉内の酸素
ガス濃度変化特性線図である。 第5図は,炉内温度と鋼材の表面酸化減量との関係を示
す線図である。 第6図は,炉内の酸素ガス濃度と炉内ガスの置換量との
関係を示す線図である。 符号の説明 1;炉体,2;加熱コイル,3;スキッド部,4;吸入
・投入口,5;採取口,6;分析計,7;制御器,8;
ガス供給装置,9;不活性ガス源,10;流量調節弁,1
1;流量計,12;吸引装置,13;真空ポンプ,14;切換
弁,15;鋼材。
FIG. 1 is an explanatory diagram showing an embodiment of the configuration of the device of the present invention. FIG. 2 is a perspective view of a furnace body showing a specific example for carrying out the function of the device of the present invention. FIG. 3 is a diagram showing the characteristics of the surface temperature of the steel material by the induction heating furnace. FIG. 4 is a supply amount change curve diagram of the inert gas into the furnace and an oxygen gas concentration change characteristic diagram in the furnace showing an example of the control operation by the device of the present invention. FIG. 5 is a diagram showing the relationship between the furnace temperature and the surface oxidation loss of steel. FIG. 6 is a diagram showing the relationship between the oxygen gas concentration in the furnace and the replacement amount of the gas in the furnace. DESCRIPTION OF SYMBOLS 1; Furnace body, 2; Heating coil, 3; Skid part, 4; Suction / inlet port, 5; Sampling port, 6; Analyzer, 7; Controller, 8;
Gas supply device, 9; Inert gas source, 10; Flow control valve, 1
1; flow meter, 12; suction device, 13; vacuum pump, 14; switching valve, 15; steel material.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】鋼材を雰囲気ガス中で再加熱する誘導加熱
炉内に加熱鋼材を挿入しそして密閉した後に前記炉内ガ
スを吸引排出する吸引装置と,該吸引装置による炉内ガ
ス吸引排出操作後に不活性ガスの雰囲気ガスを前記炉内
に供給するガス供給装置と,前記炉内の酸素ガス濃度を
分析検出する分析計と,該分析計の分析結果信号に従っ
て前記炉内の酸素ガス濃度を予め設定された一定値以下
にすべく前記ガス供給装置の炉内に対する雰囲気ガス供
給量を制御する制御器とを具備して成る誘導加熱炉の炉
内雰囲気制御装置。
1. A suction device for sucking and discharging the furnace gas after inserting and sealing the heated steel material into an induction heating furnace for reheating the steel material in an atmospheric gas, and a furnace gas suction and discharge operation by the suction device. A gas supply device for supplying an inert gas atmosphere gas into the furnace later, an analyzer for analyzing and detecting the oxygen gas concentration in the furnace, and an oxygen gas concentration in the furnace according to the analysis result signal of the analyzer. A furnace atmosphere control device for an induction heating furnace, comprising: a controller for controlling an amount of atmosphere gas supplied to the furnace of the gas supply device so as to be equal to or less than a preset constant value.
JP59156770A 1984-07-27 1984-07-27 Atmosphere control device for induction heating furnace Expired - Lifetime JPH0612709B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59156770A JPH0612709B2 (en) 1984-07-27 1984-07-27 Atmosphere control device for induction heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59156770A JPH0612709B2 (en) 1984-07-27 1984-07-27 Atmosphere control device for induction heating furnace

Publications (2)

Publication Number Publication Date
JPS6134883A JPS6134883A (en) 1986-02-19
JPH0612709B2 true JPH0612709B2 (en) 1994-02-16

Family

ID=15634931

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59156770A Expired - Lifetime JPH0612709B2 (en) 1984-07-27 1984-07-27 Atmosphere control device for induction heating furnace

Country Status (1)

Country Link
JP (1) JPH0612709B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0718157Y2 (en) * 1989-03-14 1995-04-26 中部電力株式会社 Induction heating device
JP2019157163A (en) * 2018-03-08 2019-09-19 Ntn株式会社 Heat treatment method and heat treatment apparatus for workpiece

Also Published As

Publication number Publication date
JPS6134883A (en) 1986-02-19

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