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JPH0120357B2 - - Google Patents
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JPH0120357B2 - - Google Patents

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Publication number
JPH0120357B2
JPH0120357B2 JP60075961A JP7596185A JPH0120357B2 JP H0120357 B2 JPH0120357 B2 JP H0120357B2 JP 60075961 A JP60075961 A JP 60075961A JP 7596185 A JP7596185 A JP 7596185A JP H0120357 B2 JPH0120357 B2 JP H0120357B2
Authority
JP
Japan
Prior art keywords
preheating
furnace
preheating furnace
scrap
finishing
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
Application number
JP60075961A
Other languages
Japanese (ja)
Other versions
JPS61235681A (en
Inventor
Toshio Mori
Seiji Masumoto
Shigeru Nagahata
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.)
Yoshikawa Kogyo Co Ltd
Original Assignee
Yoshikawa Kogyo 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 Yoshikawa Kogyo Co Ltd filed Critical Yoshikawa Kogyo Co Ltd
Priority to JP60075961A priority Critical patent/JPS61235681A/en
Publication of JPS61235681A publication Critical patent/JPS61235681A/en
Publication of JPH0120357B2 publication Critical patent/JPH0120357B2/ja
Granted 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
    • Y02P10/20Recycling

Landscapes

  • Furnace Details (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、製鋼用原料、特に、スクラツプの予
熱方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for preheating raw materials for steelmaking, particularly scrap.

〔従来の技術〕[Conventional technology]

電気炉、或いは転炉等の製鋼炉による鋼製造に
おいては、製鋼炉よりの発生熱の有効利用、或い
は製鋼効率の改善等を狙いとして、これら製鋼炉
に装入されるスクラツプを予熱することが種々研
究され、多くの予熱手段及び予熱装置が開発さ
れ、例えば実公昭56−23677号、特公昭56−26684
号、或いは特開昭59−66687号公報等により発表
されている。
When manufacturing steel using steelmaking furnaces such as electric furnaces or converters, it is necessary to preheat the scrap charged into these steelmaking furnaces in order to effectively utilize the heat generated by the steelmaking furnace or to improve steelmaking efficiency. Various studies have been conducted and many preheating means and preheating devices have been developed, such as Utility Model Publication No. 56-23677 and Japanese Patent Publication No. 56-26684.
No. 59-66687, or Japanese Patent Application Laid-open No. 59-66687.

これら公報の発表において、例えば、実公昭56
−23677号公報では、予熱容器内でスクラツプを
直火予熱するに際して、予熱容器よりの排出ガス
の一部を循環使用する予熱装置が提案され、ま
た、特公昭56−26684号公報では、転炉で発生す
る高温の非酸化性ガスによる転炉装入鉄原料の予
熱方法が提案され、また特開昭59−66687号公報
では、電気炉排出の高温ガスにより、空気等の清
浄なガスを熱交換器中で加熱し、更に必要に応じ
て燃焼器中で熱補充した加熱ガスによつてスキツ
プ中のスクラツプを予熱することが提案されてい
る。
In the publication of these gazettes, for example,
In Japanese Patent Publication No. 23677, a preheating device was proposed that circulated and used part of the exhaust gas from the preheating container when scrap was preheated in the preheating container. A method for preheating raw material for charging iron into a converter using high-temperature non-oxidizing gas generated in an electric furnace has been proposed, and in Japanese Patent Application Laid-open No. 1983-66687, a method for heating clean gas such as air using high-temperature gas discharged from an electric furnace has been proposed. It has been proposed to preheat the scrap in the skip with heated gas heated in an exchanger and optionally supplemented with heat in a combustor.

これらの公知のスクラツプ予熱手段によれば、
電気炉等から排出される高温ガスの熱量は、或る
程度有効に利用することができるが、スクラツプ
の加熱は、炉の操業状態に左右され、不安定であ
るとともに、含有粉塵の影響等の問題があり、ま
た、スクラツプの加熱が別の熱源による時は、十
分な熱効率を得ることはできない。
According to these known scrap preheating means,
The heat of high-temperature gas discharged from electric furnaces, etc. can be used effectively to a certain extent, but heating of scrap depends on the operating conditions of the furnace and is unstable, as well as being affected by the effects of contained dust, etc. There are problems and insufficient thermal efficiency can be obtained when the scrap heating is done by a separate heat source.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明は上記のような問題点を解決した、優れ
た熱効率と安定したスクラツプ予熱を得ることが
できるスクラツプの予熱方法を提供することを目
的とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a scrap preheating method that solves the above-mentioned problems and can obtain excellent thermal efficiency and stable scrap preheating.

〔課題を解決するための手段〕 本発明のスクラツプの予熱方法は、分岐管を介
して連結され、更に、熱ガス導入管及び通過ガス
による空気予熱器を有する排ガス管に開閉弁を介
して並列に接続された複数のスクラツプ予熱炉
を、1次予熱炉、2次予熱炉、及び仕上予熱炉と
なし、仕上予熱炉に熱ガスを導入して該炉内のス
クラツプを仕上温度に加熱し、その排ガスを1次
予熱炉、2次予熱炉に分配通入して炉内スクラツ
プを予熱し、ついで仕上予熱炉の熱スクラツプを
冷スクラツプと交換して、これを1次予熱炉とす
るとともに、前回の1次予熱炉を2次予熱炉、2
次予熱炉を仕上予熱炉とするために熱ガスを導入
することを特徴とする。
[Means for Solving the Problems] The method for preheating scrap according to the present invention is to connect a hot gas inlet pipe and an exhaust gas pipe having an air preheater using passing gas in parallel via an on-off valve. A plurality of scrap preheating furnaces connected to the furnace are used as a primary preheating furnace, a secondary preheating furnace, and a finishing preheating furnace, and hot gas is introduced into the finishing preheating furnace to heat the scrap in the furnace to a finishing temperature, The exhaust gas is distributed and passed through the primary preheating furnace and the secondary preheating furnace to preheat the scrap in the furnace, and then the hot scrap in the finishing preheating furnace is replaced with cold scrap, which is used as the primary preheating furnace. Change the previous primary preheating furnace to the secondary preheating furnace, 2
It is characterized in that hot gas is introduced in order to use the secondary preheating furnace as a final preheating furnace.

〔実施例〕〔Example〕

以下、添付図面を参照して説明する。 The following description will be made with reference to the accompanying drawings.

第1図は本発明に係るスクラツプの予熱方法を
実施するための予熱プラントの一例を示す概略構
成説明図である。
FIG. 1 is a schematic structural explanatory diagram showing an example of a preheating plant for implementing the scrap preheating method according to the present invention.

第1図において、1はスクラツプの予熱炉であ
つて、内面が断熱材で形成された殻構造をもつた
予熱炉等任意の構造とすることができる。
In FIG. 1, reference numeral 1 denotes a scrap preheating furnace, which may have any structure such as a preheating furnace with a shell structure whose inner surface is made of a heat insulating material.

本発明において、予熱炉1は、2ケ以上、好ま
しくは3ケ以上並列に配置することが必要であ
る。第1図においては、予熱炉1は3ケの予熱炉
1a,1b及び1cとからなり、かく予熱炉1
a,1b及び1cは、それぞれ、一方の炉端に高
温ガス通入孔2a,2b,2c及び廃ガス排出孔
3a,3b,3cがそれぞれ設けられる。
In the present invention, it is necessary to arrange two or more preheating furnaces 1, preferably three or more in parallel. In FIG. 1, the preheating furnace 1 consists of three preheating furnaces 1a, 1b, and 1c, and thus the preheating furnace 1
A, 1b and 1c are respectively provided with high temperature gas inlet holes 2a, 2b and 2c and waste gas discharge holes 3a, 3b and 3c at one end of the furnace.

また、予熱炉1a,1b,1cの他方端は、連
結管4により分岐管5a,5b,5cを介して連
結される。
Further, the other ends of the preheating furnaces 1a, 1b, 1c are connected by a connecting pipe 4 via branch pipes 5a, 5b, 5c.

また、高温ガス通入孔2a,2b,2cは、燃
焼装置6に接続される。なお、本発明において、
予熱炉1の高温ガス通入孔2a,2b,2cに
は、燃焼装置6で発生せしめた燃焼ガスを導入管
を介して導入するごとくなしたが、バーナーを直
結して、直接に燃焼ガスを炉内に噴入することも
できる。
Further, the high temperature gas inlet holes 2a, 2b, 2c are connected to the combustion device 6. In addition, in the present invention,
Although the combustion gas generated by the combustion device 6 is introduced into the high-temperature gas inlet holes 2a, 2b, and 2c of the preheating furnace 1 through an introduction pipe, it is also possible to directly connect a burner and introduce the combustion gas directly. It can also be injected into the furnace.

また、廃ガス排出孔3a,3b,3cはバルブ
7a,7b,7cを介して廃ガス排出管8に連結
される。
Furthermore, the exhaust gas exhaust holes 3a, 3b, and 3c are connected to the exhaust gas exhaust pipe 8 via valves 7a, 7b, and 7c.

上記廃ガス排出管8はさらに、熱交換器9を介
して放散塔10へ連結されている。
The waste gas discharge pipe 8 is further connected to a stripping tower 10 via a heat exchanger 9.

熱交換器9においては、前記燃焼装置6に導入
すべき燃焼用空気を導入し、同空気を前記廃ガス
との熱交換により予熱させる。11はその予熱空
気導管である。
In the heat exchanger 9, combustion air to be introduced into the combustion device 6 is introduced, and the air is preheated by heat exchange with the waste gas. 11 is its preheated air conduit.

本発明において、予熱炉1中で予熱されるスク
ラツプに付着する可燃物よりの可燃ガスが廃ガス
中に混合する場合は、熱交換器9の前面において
廃ガス排出管8に燃焼装置(図示せず)を介在さ
せ、その燃焼熱をも熱交換器において有効に活用
することもできる。12は燃料ガス管であつて、
任意の燃料源(回示せず)よりの燃料ガスを燃焼
装置6へ供給するごとく連結される。
In the present invention, when combustible gas from combustible materials adhering to the scrap preheated in the preheating furnace 1 is mixed into the waste gas, a combustion device (not shown) is connected to the waste gas discharge pipe 8 in front of the heat exchanger 9. ), and the combustion heat can also be effectively utilized in the heat exchanger. 12 is a fuel gas pipe,
The combustion device 6 is connected to supply fuel gas from an arbitrary fuel source (not shown) to the combustion device 6.

11a,11b,11c及び12a,12b,
12cは予熱空気導管11、燃料ガス管12と各
予熱炉1a,1b,1cとの連結管に設けられた
バルブである。
11a, 11b, 11c and 12a, 12b,
12c is a valve provided in a connecting pipe between the preheating air conduit 11, the fuel gas pipe 12, and each of the preheating furnaces 1a, 1b, and 1c.

上記の予熱プラントにおいて、スクラツプスキ
ツプ或いはクラツプシユート等予熱すべきスクラ
ツプを収容する容器(回示せず)をそれぞれの予
熱炉1a,1b,1cに装入する。かくて、例え
ば、予熱炉1aを仕上予熱炉、1bを二次予熱
炉、1cを一次予熱炉とするとき、燃焼装置6を
予熱炉1aに設定し、燃焼ガス及び予熱空気の導
入のために導管設定を行う、即ち、バルブ11
a,12aを開き、バルブ11b,11c及び1
2b,12cを閉ざし、燃焼装置6へ燃料及び燃
焼用空気の供給を行う。
In the above preheating plant, containers (not shown) containing scrap to be preheated, such as scrap skips or scrap shoots, are charged into the respective preheating furnaces 1a, 1b, and 1c. Thus, for example, when the preheating furnace 1a is the finishing preheating furnace, 1b is the secondary preheating furnace, and 1c is the primary preheating furnace, the combustion device 6 is set to the preheating furnace 1a, and for introducing combustion gas and preheating air. Conduit settings, i.e. valve 11
a, 12a, and open valves 11b, 11c and 1.
2b and 12c are closed, and fuel and combustion air are supplied to the combustion device 6.

一方、廃ガス排出管8への連結管のバルブ7
a,7b及び7c中、仕上予熱炉1a付設のバル
ブ7aは閉とし、二次予熱炉1b、一次予熱炉1
cのそれぞれのバルブ7b,7cをいずれも開と
する。
On the other hand, the valve 7 of the connecting pipe to the waste gas discharge pipe 8
In a, 7b and 7c, the valve 7a attached to the finishing preheating furnace 1a is closed, and the secondary preheating furnace 1b and the primary preheating furnace 1 are closed.
Both valves 7b and 7c of c are opened.

また、それぞれの予熱炉1a,1b,1cの他
端側における連結分岐管5a,5b,5cのそれ
ぞれのバルブは開とする。
Further, the valves of the connecting branch pipes 5a, 5b, 5c at the other ends of the preheating furnaces 1a, 1b, 1c are open.

その後、仕上予熱炉1aへ燃焼装置6より高温
ガス通入孔2aを通して燃焼高温ガスを通入し、
スクラツプを所定予熱温度、例えば300〜500℃の
温度に加熱する。
After that, the combustion high temperature gas is introduced from the combustion device 6 into the finishing preheating furnace 1a through the high temperature gas inlet 2a,
The scraps are heated to a predetermined preheating temperature, for example 300-500°C.

しかし、この仕上予熱炉1aより排出される排
出ガスは当該炉内において、その有する顕熱をス
クラツプに与えたとはいえ、例えば800℃前後の
末だ相当の高熱を有するために、連結管4を通じ
て二次予熱炉1b及び一次予熱炉1cに分配さ
れ、それぞれに収容されているスクラツプを予熱
する。
However, although the exhaust gas discharged from the finishing preheating furnace 1a imparts its sensible heat to the scrap in the furnace, it has a considerably high heat of around 800°C, for example, so it is passed through the connecting pipe 4. It is divided into a secondary preheating furnace 1b and a primary preheating furnace 1c, and preheats the scraps stored in each.

一次予熱炉1c、二次予熱炉1bにおいてそれ
ぞれ収容されているスクラツプを、例えば80℃、
180℃に予熱して温度降下し、例えば260℃、450
℃となつたガスは、廃ガス排出孔3b,3cを通
じ、共通の廃ガス排出管8を経て熱交換器9に導
入され、燃焼装置6へ供給される燃焼空気を、例
えば、250℃から300℃に予熱後、放散塔10から
排出される。
The scraps stored in the primary preheating furnace 1c and the secondary preheating furnace 1b are heated to 80°C, for example.
Preheat to 180℃ and lower the temperature, e.g. 260℃, 450℃
The gas that has reached a temperature of After preheating to ℃, it is discharged from the stripping tower 10.

上記予熱作業において、仕上予熱炉1aにおけ
るスクラツプが電気炉、或いは転炉等の操業条件
によつて予め定められた予熱温度に達した時、当
該予熱作業は終了し、ついで仕上予熱炉1a内の
予熱スクラツプを取り出し、新たに冷スクラツプ
を装入し、これを次回予熱作業の一次予熱炉と
し、廃ガス排出管8へのバルブ7aを開くととも
に、燃焼装置6を二次予熱炉1bの高温ガス通入
孔2bに連結し、廃ガス排出管8へのバルブ7b
を閉ざすとともに、バルブ11b,12bを開い
て燃焼装置6aを作動させる。
In the above preheating work, when the scrap in the finishing preheating furnace 1a reaches a preheating temperature predetermined according to the operating conditions of the electric furnace or converter, etc., the preheating work is completed, and then the scrap in the finishing preheating furnace 1a The preheating scrap is taken out, a new cold scrap is charged, and this is used as the primary preheating furnace for the next preheating operation.The valve 7a to the waste gas discharge pipe 8 is opened, and the combustion device 6 is turned into the high temperature gas of the secondary preheating furnace 1b. A valve 7b connected to the inlet hole 2b and connected to the waste gas discharge pipe 8
At the same time, the valves 11b and 12b are opened to operate the combustion device 6a.

また、一次予熱炉1cは二次予熱炉に格上げさ
れる。
Further, the primary preheating furnace 1c is upgraded to a secondary preheating furnace.

なお、スクラツプ交換時には、予熱炉1b,1
cの放冷を防ぐために、連結分岐管5b,5cの
バルブ及び廃ガス排出管8へのバルブ7b,7c
は閉じておくのが好ましい。
In addition, when replacing the scrap, the preheating furnaces 1b, 1
In order to prevent cooling of the pipes c, valves of the connecting branch pipes 5b and 5c and valves 7b and 7c to the waste gas discharge pipe 8 are installed.
It is preferable to keep it closed.

かくて、前回同様のスクラツプ予熱作業を行
い、今回予熱作業における仕上予熱炉1b中のス
クラツプを所定の予熱温度とする。
Thus, the same scrap preheating operation as last time is performed, and the scrap in the finishing preheating furnace 1b in this preheating operation is brought to a predetermined preheating temperature.

この時、一次予熱炉1a、二次予熱炉1c内の
スクラツプは、それぞれ前回と同様の予熱温度を
得ることができるものである。
At this time, the scraps in the primary preheating furnace 1a and the secondary preheating furnace 1c can each obtain the same preheating temperature as the previous time.

今回の予熱作業終了後は、前回同様の予熱炉切
り換えを順次行い、新たな予熱作業を行う。
After the current preheating work is completed, the preheating furnaces will be switched sequentially in the same way as the previous time, and a new preheating work will be performed.

仕上予熱炉に通入される高温ガス発生のための
燃焼装置6は、上記のごとき、移動形式に限るも
のではなく、各炉固定形式とすることもできる。
The combustion device 6 for generating high-temperature gas that is passed through the finishing preheating furnace is not limited to the movable type as described above, but may be of a fixed type in each furnace.

本発明において、また、スクラツプに付着する
油脂等の可燃物の気化により排ガス中に可燃成分
が存在するときは、必要に応じて熱交換器9前に
おいて燃焼装置を付設して焼却するとともに、そ
の燃焼熱を燃焼用空気の予熱に利用することもで
きる。
In the present invention, when combustible components are present in the exhaust gas due to vaporization of combustible substances such as oils and fats that adhere to the scrap, a combustion device is installed in front of the heat exchanger 9 as necessary to incinerate the waste. The heat of combustion can also be used to preheat the combustion air.

上記、第1図に示す予熱プラントによる予熱方
法は以下のとおりである。
The preheating method using the preheating plant shown in FIG. 1 above is as follows.

予熱作業の開始に当たつて、並列に設けた3個
の予熱炉1a,1b,1cにそれぞれスクラツプ
を装入するとともに、それぞれの予熱炉1a,1
b,1cを任意に定める、本例においては、第2
図イの如く、先ず、1aを仕上予熱炉、1bを二
次予熱炉、1cを一次予熱炉と定め、仕上予熱炉
1aに燃焼装置6を設定作動させるとともに、バ
ルブ7aを閉とする。一方、二次予熱炉1b、一
次予熱炉1cの廃ガス排出管8へのバルブ7b,
7cは開き、予熱作業を行う。
At the start of the preheating work, scrap is charged into each of the three preheating furnaces 1a, 1b, 1c installed in parallel, and each of the preheating furnaces 1a, 1
b, 1c are arbitrarily determined. In this example, the second
As shown in Figure A, first, 1a is designated as a finishing preheating furnace, 1b is a secondary preheating furnace, and 1c is a primary preheating furnace.The combustion device 6 is set and operated in the finishing preheating furnace 1a, and the valve 7a is closed. On the other hand, a valve 7b to the waste gas discharge pipe 8 of the secondary preheating furnace 1b and the primary preheating furnace 1c,
7c is opened to perform preheating work.

燃焼装置6よりの高温ガスは、1200℃の温度で
仕上予熱炉1a内に通入され、装入スクラツプを
加熱する。この加熱中における仕上予熱炉1aよ
りの排出ガスは、なお、850℃の高温を有し、連
結管4を通じて矢印13のごとく二次予熱炉1b
及び一次予熱炉1cにそれぞれ均等に配分通入さ
せる。
The hot gas from the combustion device 6 is passed into the finishing preheating furnace 1a at a temperature of 1200°C to heat the charging scrap. During this heating, the exhaust gas from the finishing preheating furnace 1a still has a high temperature of 850°C, and passes through the connecting pipe 4 as shown by the arrow 13 to the secondary preheating furnace 1b.
and the primary preheating furnace 1c in an even distribution.

そのときの配分量は、必ずしも均等である必要
はなく、任意に定めることができる。
The distribution amount at that time does not necessarily have to be equal and can be determined arbitrarily.

ついで、それぞれの廃ガスは、共通の廃ガス排
出管8内にて混合し、450℃の温度で矢印14方
向に熱交換器9へ通入される。
The respective waste gases are then mixed in a common waste gas discharge pipe 8 and passed into a heat exchanger 9 in the direction of arrow 14 at a temperature of 450°C.

一方、熱交換器9には燃焼用空気が導入され、
相互熱交換され、燃焼用空気は250℃に予熱され
た。一方、熱交換器9を出て300℃の温度で放散
塔10より放出した。
On the other hand, combustion air is introduced into the heat exchanger 9,
There was mutual heat exchange and the combustion air was preheated to 250°C. On the other hand, it exited the heat exchanger 9 and was discharged from the stripping tower 10 at a temperature of 300°C.

上記予熱作業において、仕上予熱炉1aのスク
ラツプは、400℃に、二次予熱炉1bのスクラツ
プは180℃に、また一次予熱炉1cのスクラツプ
は80℃にそれぞれ予熱された。
In the above preheating operation, the scrap in the finishing preheating furnace 1a was preheated to 400°C, the scrap in the secondary preheating furnace 1b was preheated to 180°C, and the scrap in the primary preheating furnace 1c was preheated to 80°C.

この時のそれぞれの炉よりの廃ガス温度はそれ
ぞれ470℃、430℃であり、廃ガス排出管8中で混
合し、熱交換器9の入口では400℃であつた。
At this time, the temperature of the waste gas from each furnace was 470°C and 430°C, respectively, and was mixed in the waste gas discharge pipe 8, and the temperature at the inlet of the heat exchanger 9 was 400°C.

仕上予熱炉1a内のスクラツプが所定の予熱温
度に到着後、予熱作業を中断し、仕上予熱炉内の
スクラツプを取り出し、新たに冷スクラツプを装
入後、これを一次予熱炉とするとともに、前回二
次予熱炉を仕上予熱炉、前回一次予熱炉を二次予
熱炉として第2図ロの如き、ガス流れによりスク
ラツプ予熱を行つた。
After the scrap in the finishing preheating furnace 1a reaches a predetermined preheating temperature, the preheating operation is interrupted, the scrap in the finishing preheating furnace is taken out, and a new cold scrap is charged, and this is used as the primary preheating furnace. The secondary preheating furnace was used as a finishing preheating furnace, and the previous primary preheating furnace was used as a secondary preheating furnace, as shown in FIG. 2B, and scrap preheating was performed by gas flow.

〔発明の効果〕〔Effect of the invention〕

本発明のスクラツプ予熱方法は、上記のごとく
であるので、炉内温度の低下を防いで熱媒体の保
有熱を極めて有効に利用することもでき、スクラ
ツプの如き不定形状の被加熱体をも効率的な加熱
を行うことができる。
Since the scrap preheating method of the present invention is as described above, it is possible to prevent the temperature inside the furnace from decreasing and use the heat retained in the heating medium extremely effectively, and it is also possible to efficiently heat irregularly shaped objects such as scrap. heating can be performed.

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

第1図は本発明の予熱方法を実施するための予
熱プラントの一例を示す概略構成説明図、第2図
は予熱時のガス流れ図を示す。 図中、1a,1b,1c:予熱炉、4:連結
管、6:燃焼装置、8:廃ガス排出管、9:熱交
換器。
FIG. 1 is a schematic structural explanatory diagram showing an example of a preheating plant for carrying out the preheating method of the present invention, and FIG. 2 is a gas flow diagram during preheating. In the figure, 1a, 1b, 1c: preheating furnace, 4: connecting pipe, 6: combustion device, 8: waste gas discharge pipe, 9: heat exchanger.

Claims (1)

【特許請求の範囲】[Claims] 1 分岐管を介して連結され、更に、熱ガス導入
管及び通過ガスによる空気予熱器を有する排ガス
管に開閉弁を介して並列に接続された複数のスク
ラツプ予熱炉を、1次予熱炉、2次予熱炉、及び
仕上予熱炉となし、仕上予熱炉に熱ガスを導入し
て該炉内のスクラツプを仕上温度に加熱し、その
排ガスを1次予熱炉、2次予熱炉に分配通入して
炉内スクラツプを予熱し、ついで仕上予熱炉の熱
スクラツプを冷スクラツプと交換して、これを1
次予熱炉とするとともに、前回の1次予熱炉を2
次予熱炉、2次予熱炉を仕上予熱炉とするために
熱ガスを導入することを特徴とするスクラツプの
予熱方法。
1 A plurality of scrap preheating furnaces are connected in parallel via on-off valves to a hot gas inlet pipe and an exhaust gas pipe having an air preheater using passing gas, which are connected via branch pipes, and a primary preheating furnace, 2 A secondary preheating furnace and a finishing preheating furnace are used. Hot gas is introduced into the finishing preheating furnace to heat the scrap in the furnace to the finishing temperature, and the exhaust gas is distributed to the primary preheating furnace and the secondary preheating furnace. preheat the scrap in the furnace, then replace the hot scrap in the finishing preheating furnace with cold scrap, and
In addition to using the secondary preheating furnace, the previous primary preheating furnace is used as the second preheating furnace.
A method for preheating scrap characterized by introducing hot gas into the secondary preheating furnace and the secondary preheating furnace to serve as a finishing preheating furnace.
JP60075961A 1985-04-10 1985-04-10 Method of preheating scrap Granted JPS61235681A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60075961A JPS61235681A (en) 1985-04-10 1985-04-10 Method of preheating scrap

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60075961A JPS61235681A (en) 1985-04-10 1985-04-10 Method of preheating scrap

Publications (2)

Publication Number Publication Date
JPS61235681A JPS61235681A (en) 1986-10-20
JPH0120357B2 true JPH0120357B2 (en) 1989-04-17

Family

ID=13591323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60075961A Granted JPS61235681A (en) 1985-04-10 1985-04-10 Method of preheating scrap

Country Status (1)

Country Link
JP (1) JPS61235681A (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5823552B2 (en) * 1980-03-07 1983-05-16 川崎重工業株式会社 Multiple bucket type material preheating device

Also Published As

Publication number Publication date
JPS61235681A (en) 1986-10-20

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