JPS6318016A - Method and equipment for melting iron-based scrap - Google Patents
Method and equipment for melting iron-based scrapInfo
- Publication number
- JPS6318016A JPS6318016A JP61161635A JP16163586A JPS6318016A JP S6318016 A JPS6318016 A JP S6318016A JP 61161635 A JP61161635 A JP 61161635A JP 16163586 A JP16163586 A JP 16163586A JP S6318016 A JPS6318016 A JP S6318016A
- Authority
- JP
- Japan
- Prior art keywords
- scrap
- furnace
- exhaust gas
- iron
- shaft furnace
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Furnace Details (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は、鉄系スクラップの溶解方法及びその溶解装
置の改良に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for melting iron-based scrap and an improvement in a melting apparatus for the same.
(従来技術)
従来石炭等の炭材を燃料源とした鉄系スクラップ溶解プ
ロセスとして、転炉型の溶解炉を利用したプロセスが種
々報告されている。この方法は、転炉内に鉄系スクラッ
プを挿入し、転炉下部からコークス、微粉炭を酸素等と
ともに吹込み、転炉上部から酸素を吹込んで、鉄系スク
ラップを溶解している。しかしこの方法は、コークス等
を比較的多く必要とし、コストガ高い。また炉の構造上
バッチ式で操業するので、操業効率に問題がある。(Prior Art) Various processes using a converter-type melting furnace have been reported as conventional iron-based scrap melting processes using carbonaceous materials such as coal as a fuel source. In this method, iron-based scrap is inserted into a converter, coke and pulverized coal are blown in from the bottom of the converter along with oxygen, and oxygen is blown in from the top of the converter to melt the ferrous scrap. However, this method requires a relatively large amount of coke, etc., and is expensive. Additionally, because the furnace is operated in batch mode due to its structure, there is a problem with operational efficiency.
第2図に示す公知のシャフト炉1では、上部に配置した
ホッパ2から鉄系スクラップ3を一定轟充填したのち溶
解反応炉4から発生した高温ガスをシャフト炉1の上部
から供給し、充填しである鉄系スクラップと熱交換して
予熱し、しかる後ロスドル型ダンパを開いて鉄系スクラ
ップを溶融炉6に投入し、この溶融炉6で酸素、微粉炭
、アルゴン等を吹込んで鉄系スクラップを溶解している
。In the known shaft furnace 1 shown in FIG. 2, iron-based scrap 3 is charged at a constant rate from a hopper 2 placed at the top, and then high-temperature gas generated from a melting reactor 4 is supplied from the top of the shaft furnace 1 to fill the furnace. After that, the Rosdol type damper is opened and the iron scrap is put into the melting furnace 6, where oxygen, pulverized coal, argon, etc. are blown into the iron scrap. is dissolved.
しかしこの方法はバッチ式であり連続操業ができない。However, this method is a batch method and cannot be operated continuously.
しかも原料を保持する耐熱性のロスドル型ダンパー5が
必要であが、シャフト炉の高温に耐えうる材質のダンパ
ーはない。Moreover, a heat-resistant Rossdol type damper 5 is required to hold the raw material, but there is no damper made of a material that can withstand the high temperatures of a shaft furnace.
(発明が解決しようとする技術的課題)本発明は、鉄系
スクラップを連続的に高温に予熱して製造コストを下げ
ることができ、しかも耐熱性のロスドルを必要としない
鉄系スクラップの溶解方法及び溶解装置を提供すること
を目的とする。(Technical Problems to be Solved by the Invention) The present invention provides a method for melting iron-based scrap that can reduce manufacturing costs by continuously preheating iron-based scrap to a high temperature, and that does not require a heat-resistant loss dollar. and a dissolving device.
(技術的課題を解決するための手段)
即ちこの発明は、シャフト炉の上部から下部に向けて高
温ガスを流通せしめるとともにシャフト炉下部から鉄系
スクラップを連続的に供給して高温ガスと対向流で熱交
換して後、予熱されたシャフト炉上部の鉄系スクラップ
を溶融炉に投入して溶解する鉄系スクラップの溶解方法
、及びシャフト炉の上部に高温ガス供給口を形成し、シ
ャフト炉の下部に排ガス又は燃料用化学用ガスの出口を
形成し、かつシャフト炉下部に原料連続供給機構を配置
し、更に上記シャフト炉の上部に溶融炉を連通してなる
鉄系スクラップの溶解装置である。(Means for Solving Technical Problems) That is, the present invention allows high-temperature gas to flow from the upper part to the lower part of the shaft furnace, and continuously supplies iron-based scrap from the lower part of the shaft furnace to counter-flow the high-temperature gas. A method for melting iron scrap in which the preheated iron scrap in the upper part of a shaft furnace is charged into a melting furnace and melted after heat exchange, and a high temperature gas supply port is formed in the upper part of the shaft furnace. This iron-based scrap melting device has an outlet for exhaust gas or fuel chemical gas in the lower part, a continuous raw material supply mechanism in the lower part of the shaft furnace, and a melting furnace connected to the upper part of the shaft furnace. .
(発明の効果)
この発明によれば、鉄系スクラップが下部から上部に移
動している間に高温ガスで予熱されるので、高温に予熱
された鉄系スクラップが最上部に位置することとなる。(Effect of the invention) According to this invention, since the iron-based scrap is preheated with high-temperature gas while moving from the bottom to the top, the iron-based scrap that has been preheated to a high temperature is located at the top. .
従ってこの鉄系スクラップは、シャフト炉下部の鉄系ス
クラップの荷重を受けず、この結果鉄系スクラップを軟
化温度付近まで高温に予熱することができる。また鉄系
スクラップを連続的に供給できるので、鉄系スクラップ
の加熱効率が良い。さらに高温に予熱された鉄系スクラ
ップは上部にあり、下部はあまり加熱されていないので
耐火性のロスドルを必要としない。Therefore, this iron-based scrap is not subjected to the load of the iron-based scrap in the lower part of the shaft furnace, and as a result, the iron-based scrap can be preheated to a high temperature close to its softening temperature. Moreover, since iron-based scrap can be continuously supplied, the heating efficiency of iron-based scrap is good. Furthermore, the iron-based scrap that has been preheated to a high temperature is in the upper part, and the lower part is not heated so much that there is no need for refractory rosdol.
(実施例)
以下この発明を第1図に示す実施例を参照して説明する
。シャフト炉11は、上部に高温ガス供給口12を形成
し、下部に排ガス出口13を形成するとともに鉄系スク
ラップ連続供給機構14を配置している。高温ガス供給
口12は、高温ガス流路管15を介して溶融炉16の上
部に連通している。溶融炉16は、上部から予熱した鉄
系スクラップを入れ底部から酸素ガス、微粉炭等の燃料
、キャリアガス、石灰を吹込み、鉄系スクラップを溶融
する。この溶融炉16からは、CO十GO2の組成を主
成分とする高温ガス(約1800℃)が発生する。上記
流路管15の外周には熱回収用ボイラ17が配置されて
いる。上記シャフト炉11の上部には、鉄系スクラップ
押し出しシリンダ18が取付けられ、シャフト炉上部の
予熱された鉄系スクラップ19(1400℃程度に予熱
されている。)を流路管15方向へ押出せるようになっ
ている。また排ガス出口13には、排ガス管20が取付
けられ、この排ガス管20に排ガスブロワ21(又は排
圧タービン)、圧力検出器22及びガス成分分析器23
がそれぞれ装着されている。流路管15及びシャフト炉
11の中央部分には、複数本の吹出し管24が取付けら
れ、これら管からガス、オイル、微粉炭等の燃料や空気
、酸素等を供給可能の様にして排ガスを燃焼させ、スク
ラップを予熱できるようにしてもよい。シャフト炉11
の下部に設けた鉄系スクラップ連続供給機構14は、底
部に鉄系スクラップ押し上げシリンダ25を設け、その
上部に開閉自在な鉄系スクラップ支持板26を設け、更
にシリンダ25と支持板26との間の側面に鉄系スクラ
ップ供給口27を設けて構成されている。(Example) The present invention will be described below with reference to an example shown in FIG. The shaft furnace 11 has a high temperature gas supply port 12 formed in the upper part, an exhaust gas outlet 13 formed in the lower part, and a continuous iron scrap supply mechanism 14 arranged therein. The high temperature gas supply port 12 communicates with the upper part of the melting furnace 16 via the high temperature gas flow pipe 15. The melting furnace 16 receives preheated iron scrap from the top and blows oxygen gas, fuel such as pulverized coal, carrier gas, and lime from the bottom to melt the iron scrap. This melting furnace 16 generates high-temperature gas (approximately 1800° C.) whose main components are CO and GO2. A heat recovery boiler 17 is arranged around the outer periphery of the flow pipe 15 . A ferrous scrap extrusion cylinder 18 is attached to the upper part of the shaft furnace 11, and can extrude preheated ferrous scrap 19 (preheated to about 1400° C.) from the upper part of the shaft furnace toward the flow pipe 15. It looks like this. Further, an exhaust gas pipe 20 is attached to the exhaust gas outlet 13, and the exhaust gas pipe 20 includes an exhaust gas blower 21 (or exhaust pressure turbine), a pressure detector 22, and a gas component analyzer 23.
are installed on each. A plurality of blowout pipes 24 are attached to the flow pipe 15 and the center of the shaft furnace 11, and these pipes can supply fuel such as gas, oil, pulverized coal, air, oxygen, etc. to discharge exhaust gas. It may also be burned to allow the scrap to be preheated. Shaft furnace 11
The ferrous scrap continuous supply mechanism 14 provided at the bottom includes a ferrous scrap pushing up cylinder 25 at the bottom, a ferrous scrap support plate 26 that can be opened and closed above the cylinder 25, and a ferrous scrap support plate 26 that can be freely opened and closed. A steel scrap supply port 27 is provided on the side surface of the steel scrap supply port.
溶融炉16から発生した高温ガスは、流路管15を通り
、シャフト炉上部から下部に流下して排ガス管20を通
って排出される。鉄系スクラップは、供給口27からシ
リンダ25と支持板26との間に供給される。この時、
シリンダー18により高温のスクラップ19を押し出し
、支持板26を開き、同時にシリンダ25を押し上げて
鉄系スクラップ19をシャフト炉11の上部に押し上げ
る。この操作は、一定間隔ごとに間欠的に行なわれ、こ
のことにより鉄系スクラップが連続的に供給されること
となる。シャフト炉11内の鉄系スクラップ19は、上
部から下部に流動している高温排ガスと熱交換して予熱
されながら順次シャフト炉11の上部に上昇してくる。High-temperature gas generated from the melting furnace 16 passes through the flow pipe 15, flows down from the upper part of the shaft furnace to the lower part, and is discharged through the exhaust gas pipe 20. Iron-based scrap is supplied between the cylinder 25 and the support plate 26 from the supply port 27 . At this time,
The high-temperature scrap 19 is pushed out by the cylinder 18, the support plate 26 is opened, and at the same time the cylinder 25 is pushed up to push the ferrous scrap 19 to the upper part of the shaft furnace 11. This operation is performed intermittently at regular intervals, so that iron-based scrap is continuously supplied. The iron-based scrap 19 in the shaft furnace 11 gradually ascends to the upper part of the shaft furnace 11 while being preheated by exchanging heat with the high-temperature exhaust gas flowing from the upper part to the lower part.
シリンダ18は予熱された鉄系スクラップ19を押し出
し、y
流路管15から溶融炉16内に供給する。この操作は、
上記鉄系スクラップ押し上げシリンダ25に連動して間
欠的に行なう。The cylinder 18 pushes out preheated ferrous scrap 19 and supplies it into the melting furnace 16 through the y-flow pipe 15. This operation
This is performed intermittently in conjunction with the iron scrap lifting cylinder 25.
この構成及び方法によれば予熱されて約1400℃とな
った鉄系スクラップがシャフト炉11最上部にあるため
、この鉄系スクラップでシャフト炉内の鉄系スクラップ
を支持する必要がなく、これを高温に加熱できる。According to this configuration and method, since the iron-based scrap that has been preheated to about 1400°C is located at the top of the shaft furnace 11, there is no need to support the iron-based scrap in the shaft furnace with this iron-based scrap. Can be heated to high temperatures.
また溶融炉16からの高温ガスの顕熱及び潜熱を鉄系ス
クラップの予熱に有効に利用して、燃料の使用量を低く
おさえコストを低下することもできる。この場合には、
吹出し管24から酸素、空気等を吹き込み、ガス中の可
燃ガス(Go、H2、CI Hn )の一部あるいは全
部を燃焼させ、そして最終排ガス温度を200℃以下に
することもできる。また鉄系スクラップのオーバーヒー
トを防ぐためシャフト炉上部から高温ガスの一部を取出
し、他の用途に供してもよい。取り出したガスの一部を
吹出し管24に供給するガスに用いてもよい。なお吹出
し管24からの酸素、空気の供給を停止して、COを含
む排ガスを排ガス管20から取出すようにする操業も可
能である。更に溶融炉からの排ガスだけでは、鉄系スク
ラップを十分に予熱できない場合、吹出し管24から燃
料を吹き込む操業も可能である。Furthermore, the sensible heat and latent heat of the high-temperature gas from the melting furnace 16 can be effectively used to preheat the iron-based scrap, thereby reducing the amount of fuel used and lowering costs. In this case,
It is also possible to blow oxygen, air, etc. from the blow-off pipe 24 to combust some or all of the combustible gases (Go, H2, CI Hn) in the gas, and to lower the final exhaust gas temperature to 200° C. or lower. Further, in order to prevent overheating of the iron-based scrap, a portion of the high-temperature gas may be taken out from the upper part of the shaft furnace and used for other purposes. A part of the extracted gas may be used as the gas to be supplied to the blowout pipe 24. Note that it is also possible to perform an operation in which the supply of oxygen and air from the blow-off pipe 24 is stopped and exhaust gas containing CO is taken out from the exhaust gas pipe 20. Furthermore, if the iron-based scrap cannot be sufficiently preheated with only the exhaust gas from the melting furnace, an operation in which fuel is blown from the blow-off pipe 24 is also possible.
次に本発明のマテリアル70−の一例を示す。Next, an example of the material 70- of the present invention will be shown.
以下の例では、溶鋼溶製の場合を示しているが、溶銑も
炭素濃度、珪素濃度を調整することにより溶製可能であ
る。The following example shows the case of molten steel melting, but hot metal can also be melted by adjusting the carbon concentration and silicon concentration.
(スクラップ)
投入量:1103kg
予熱温度: 1400℃(シャフト炉出口)(吹込み空
気)
吹込みI:157Nm3
(溶融炉から発生するガス)
ガス温度: 1750℃
酸化度:0.55
ガス組成:C035%、CO235%、829%、82
0 19%、N22%
(溶融炉に吹込むガス等)
、酸素:86Nm3、石炭ニア2ka、キャリアガス:
5、 4Nm3
溶融炉に投入する石灰:46k。(Scrap) Input amount: 1103 kg Preheating temperature: 1400°C (shaft furnace outlet) (Blowing air) Injection I: 157 Nm3 (Gas generated from the melting furnace) Gas temperature: 1750°C Oxidation degree: 0.55 Gas composition: C035 %, CO2 35%, 829%, 82
0 19%, N22% (gas injected into the melting furnace, etc.), Oxygen: 86Nm3, Coal near 2ka, Carrier gas:
5. 4Nm3 Lime charged into the melting furnace: 46k.
(溶融炉内生成物)
溶鋼: 1000に+1(G O,05%) 、スラ
グニアkg
(スクラップ予熱後の排ガス)
流量:291Nm3
組成:C0236%、82028%、N244%温度:
ioo℃(Products in the melting furnace) Molten steel: +1 to 1000 (GO, 05%), kg of slagnia (exhaust gas after scrap preheating) Flow rate: 291 Nm3 Composition: C0236%, 82028%, N244% Temperature:
ioo℃
第1固縛本発明の1実施例を示す溶融炉の説明図、第2
図は従来例を示す説明図である。
11・・・シャフト炉、12・・・高温ガス供給口、1
3・・・排ガス出口、14・・・鉄系スクラップ連続供
給機構、15・・・高温ガス流路管、16・・・溶融炉
、17・・・熱回収用ボイラ、18・・・鉄系スクラッ
プ押出しシリンダ、19・・・鉄系スクラップ、2o排
ガス管、21・・・ブロワ、22・・・圧力検出器、2
3・・・成分分析器、24・・・吹出し管、25・・・
鉄系スクラツブ押し上げシリンダ、26・・・支持板、
27・・・鉄系スクラップ供給口First lashing Explanatory diagram of a melting furnace showing one embodiment of the present invention, Second lashing
The figure is an explanatory diagram showing a conventional example. 11...Shaft furnace, 12...High temperature gas supply port, 1
3... Exhaust gas outlet, 14... Iron-based scrap continuous supply mechanism, 15... High-temperature gas flow pipe, 16... Melting furnace, 17... Heat recovery boiler, 18... Iron-based scrap Scrap extrusion cylinder, 19... Iron scrap, 2o exhaust gas pipe, 21... Blower, 22... Pressure detector, 2
3...Component analyzer, 24...Blowout pipe, 25...
Iron-based scrubbing cylinder, 26... support plate,
27... Iron scrap supply port
Claims (2)
通せしめるとともにシャフト炉下部から鉄系スクラップ
を連続的に供給して高温ガスと対向流で熱交換した後、
予熱されたシャフト炉上部の鉄系スクラップを溶融炉に
投入して溶解する鉄系スクラップの溶解方法。(1) High-temperature gas is made to flow from the top to the bottom of the shaft furnace, and iron scrap is continuously supplied from the bottom of the shaft furnace to exchange heat with the high-temperature gas in a counterflow.
A method of melting iron-based scrap in which the iron-based scrap in the upper part of a preheated shaft furnace is charged into a melting furnace and melted.
ャフト炉の下部に排ガス又は燃料用化学用ガスの出口を
形成し、かつシャフト炉下部に原料連続供給機構を配置
し、更に上記シャフト炉上部に溶融炉を連通してなる鉄
系スクラップの溶解装置。(2) A high-temperature gas supply port is formed in the upper part of the shaft furnace, an outlet for exhaust gas or fuel chemical gas is formed in the lower part of the shaft furnace, and a raw material continuous supply mechanism is arranged in the lower part of the shaft furnace, and the shaft A device for melting iron scrap that has a melting furnace connected to the top of the furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61161635A JPS6318016A (en) | 1986-07-09 | 1986-07-09 | Method and equipment for melting iron-based scrap |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61161635A JPS6318016A (en) | 1986-07-09 | 1986-07-09 | Method and equipment for melting iron-based scrap |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6318016A true JPS6318016A (en) | 1988-01-25 |
Family
ID=15738933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61161635A Pending JPS6318016A (en) | 1986-07-09 | 1986-07-09 | Method and equipment for melting iron-based scrap |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6318016A (en) |
-
1986
- 1986-07-09 JP JP61161635A patent/JPS6318016A/en active Pending
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