JPS62116712A - Melting and smelting vessel having splash lance - Google Patents
Melting and smelting vessel having splash lanceInfo
- Publication number
- JPS62116712A JPS62116712A JP25379385A JP25379385A JPS62116712A JP S62116712 A JPS62116712 A JP S62116712A JP 25379385 A JP25379385 A JP 25379385A JP 25379385 A JP25379385 A JP 25379385A JP S62116712 A JPS62116712 A JP S62116712A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- splash
- lance
- converter
- slag
- 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
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/30—Regulating or controlling the blowing
- C21C5/35—Blowing from above and through the bath
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、鉄の溶融還元法、含Cr溶銑の製造法及びス
クラップ溶解法を実施するうえで適用されるスプラッシ
ュランスを有する溶解・製錬容器に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention is a melting and smelting process having a splash lance that is applied in carrying out an iron smelting reduction method, a Cr-containing hot metal production method, and a scrap melting method. It concerns containers.
従来、製錬プロセスにおける酸素上吹き転炉等において
は、炉内の主反応を起こさせる酸素を吹き込むランス、
もしくは羽口以外に2次燃焼用の酸素を吹き込むランス
または羽口が設けられることがあり、例えば特公昭53
−35764号記載の転炉のように、側壁に変位可能な
羽口を設けたものがある。この従来技術では溶湯内で発
生した一酸化炭素(CO)が溶湯上のスラグ中を上昇し
てスラグ層の上方に層(ゾーン)として滞留するものを
検出し、検出した一酸化炭素を基準にして側面の羽目を
水平方向又は前後に移動させ、羽口から酸素を吹き込ん
で一酸化炭素を完全に燃焼させる。したがって、スラグ
層の上方では、−酸化炭素の燃焼により高熱となるが、
湯面と高熱部分との間にはスラグ層が′存在し、しかも
スラグ層は空気を含んだ状態にあるので、高熱ば溶湯へ
伝導し難い。Conventionally, in the oxygen top-blown converter etc. in the smelting process, a lance is used to blow oxygen to cause the main reaction inside the furnace.
Alternatively, a lance or tuyere for blowing oxygen for secondary combustion may be provided in addition to the tuyere.
Some converters, such as the one described in No. 35764, are equipped with movable tuyeres on the side walls. This conventional technology detects carbon monoxide (CO) generated in the molten metal that rises in the slag above the molten metal and accumulates as a layer (zone) above the slag layer, and then uses the detected carbon monoxide as a reference. The side panels are moved horizontally or back and forth, and oxygen is blown through the tuyeres to completely burn out the carbon monoxide. Therefore, above the slag layer, high heat is generated due to the combustion of carbon oxide,
A slag layer exists between the molten metal surface and the high-temperature area, and since the slag layer contains air, high heat is difficult to conduct to the molten metal.
また、上記従来技術以外にも2次燃焼用酸素を吹き込む
穴を製錬用の酸素吹込みランスと同一のランスに別個に
設けて、その穴から2次燃焼用酸素を吹き込むものがあ
る。しかしこの場合2次燃焼の領域がランスの穴の先端
に限定され、2次燃焼効率は低い。In addition to the prior art described above, there is a method in which a hole for blowing oxygen for secondary combustion is separately provided in the same lance as an oxygen blowing lance for smelting, and oxygen for secondary combustion is blown through the hole. However, in this case, the secondary combustion area is limited to the tip of the lance hole, and the secondary combustion efficiency is low.
ところで、例えばステンレス溶湯を製造する場合には、
Cr鉱石、炭材を金属溶湯中に装入するが、この場合、
上記の製鉄の場合と異なりスラグが多量に生じる。例え
ば上記の例では、ホットメタル1トンを製造するのに約
180kgのスラグを生成するのに対し、Cr鉱還元の
場合はトン当たり約300 kgものスラグが生じる。By the way, for example, when manufacturing molten stainless steel,
Cr ore and carbonaceous material are charged into molten metal, but in this case,
Unlike the case of iron manufacturing mentioned above, a large amount of slag is produced. For example, in the above example, about 180 kg of slag is produced to produce 1 ton of hot metal, whereas about 300 kg of slag is produced per ton in the case of Cr ore reduction.
しかもこのスラグ中には未反応のCr2O3を2%位含
んでおり、これを連続的に排滓、廃棄することはコスト
面で好ましくない。したがって、Cr鉱石の還元法にお
いてはその操作は回分法によらざるを得す、その際、絶
えず増大するスラグに対し適切にスラグ液滴を飛散させ
ようとすれば、羽目の高さ調整が必要となる。Moreover, this slag contains about 2% of unreacted Cr2O3, and it is not desirable from a cost standpoint to continuously drain and dispose of this slag. Therefore, in the reduction method for Cr ore, the operation has to be carried out in batches, and in this case, in order to properly scatter slag droplets against the constantly increasing slag, it is necessary to adjust the height of the slats. becomes.
本発明に係るスプラッシュランスを有する溶解・製錬容
器は、公知の送酸ランスのほかに、1本以上のスプラッ
シュランスを可動的に炉体に設置したものである。The melting/smelting vessel having a splash lance according to the present invention has one or more splash lances movably installed in the furnace body in addition to the known oxygen supply lance.
本発明においては、溶融還元法により、例えばCr溶鉱
を製造する場合、炉体に設置された1本以上のスプラッ
シュランスがスラグあるいは金属溶湯レベルに応じて上
下動してスラグの液滴を生成、飛散させるので、常に一
定量の金属溶湯及びスラグを保持することができる。In the present invention, when producing, for example, Cr molten ore by the smelting reduction method, one or more splash lances installed in the furnace body move up and down depending on the level of slag or molten metal to generate slag droplets. Since the molten metal and slag are scattered, a certain amount of molten metal and slag can be maintained at all times.
以下、本発明の実施例について説明する。 Examples of the present invention will be described below.
第1図はこの実施例の溶解・製錬容器の概略構成図で、
第2図は第1図のI−I線における断面図である。図に
おいて、(1)は溶解・製錬容器の炉体であり、金属溶
湯(2)の脱炭精錬を行うために、金属溶湯(2)の表
面に向は酸素を吹付ける送酸ランス(3)が炉頂部より
炉内中心に挿入されている。金属溶湯(2)中には炉体
(1)の底部に多数設けられた原料装入口(4)を通し
て鉄鉱石及び炭材(石炭、コークスなどの石炭系固体炭
素質をいう)がアルゴン、酸素、あるいはプロセスガス
等とともに連続的に吹き込まれる。Figure 1 is a schematic diagram of the melting and smelting vessel of this example.
FIG. 2 is a sectional view taken along line I--I in FIG. 1. In the figure, (1) is the furnace body of the melting/smelting vessel, and in order to decarburize and refine the molten metal (2), the oxygen supply lance (1) that sprays oxygen onto the surface of the molten metal (2) 3) is inserted into the center of the furnace from the top of the furnace. Iron ore and carbonaceous materials (coal-based solid carbon materials such as coal and coke) are fed into the molten metal (2) through argon and oxygen through the raw material charging ports (4) provided at the bottom of the furnace body (1). , or continuously blown in together with process gas, etc.
さらに、炉体(1)の炉口にはスプラッシュランス(1
0)が1本以上、矢印a方向に可動的に取り付けられて
いる。第1図の場合は、3本のスブラ・ソシュランス(
10)が送酸ランス(3)と平行に上下動するよう設け
られ、かつ、第2図に示すように送酸ランス(3)を中
心として点対称に配置されている。第3図の場合は、ス
プラッシュランス(1o)が送酸ランス(3)に対し傾
斜状態で移動するよう炉体(1)の側壁に取り付けられ
ている点を除き、第1図の場合と同様である。Furthermore, a splash lance (1
0) are movably attached in the direction of arrow a. In the case of Figure 1, there are three Subra Sosurans (
10) is provided to move up and down parallel to the oxygen supply lance (3), and is arranged point-symmetrically with the oxygen supply lance (3) as the center, as shown in FIG. The case in Fig. 3 is the same as the case in Fig. 1, except that the splash lance (1o) is attached to the side wall of the furnace body (1) so as to move at an angle with respect to the oxygen supply lance (3). It is.
このスプラッシュランス(10)から吹付けられろガス
は、酸化性ガス(酸素のみ又は酸素を一部に含むガスを
いう)、当該工程で発生し回収されたプロセスガス、あ
るいはA r 、 N 2等の不活性ガスのいずれでも
よい。The gas blown from this splash lance (10) is an oxidizing gas (referring to a gas containing only oxygen or a gas partially containing oxygen), a process gas generated and recovered in the process, or Ar, N2, etc. Any inert gas may be used.
なお、送酸ランス(3)は、図示は省略するが、いわゆ
るダブルフロータイブに構成されており、酸素、石炭あ
るいはコークスを吹き込む通路と2次燃焼用酸素を吹き
込む通路を有する二重管構造となっている。さらに最外
周部には冷却水の通路が設けられている。また送酸ラン
ス(3)も矢印す方向に上下動する。Although not shown, the oxygen supply lance (3) is constructed as a so-called double flow type, with a double pipe structure having a passage for blowing oxygen, coal or coke into it and a passage for blowing oxygen for secondary combustion. It has become. Furthermore, a cooling water passage is provided at the outermost periphery. The oxygen supply lance (3) also moves up and down in the direction of the arrow.
次に、50トンの溶湯を収納可能な炉にて実施した結果
は次のとりである。Next, the following results were obtained using a furnace capable of storing 50 tons of molten metal.
予備処理された溶銑(C=約4.0%、5i=0.1%
、p=0.025%、S=0.010%。Pretreated hot metal (C=approx. 4.0%, 5i=0.1%
, p=0.025%, S=0.010%.
温度、1290℃)を炉体(1)に供給し、表1に示す
諸元にてCr鉱石の溶融還元を行い、48トンの含Cr
溶銑を製造した。Temperature: 1290°C) was supplied to the furnace body (1), and Cr ore was melted and reduced according to the specifications shown in Table 1, and 48 tons of Cr-containing
Produced hot metal.
溶製された含Cr溶銑の成分は、C=5.9%。The component of the produced Cr-containing hot metal is C=5.9%.
Cr=18.2%、溶湯f昂度(よ1620℃であった
。Cr=18.2%, molten metal temperature (1620°C).
表1
含Cri容銑1トン当り
〔発明の効果〕
以上のように、本発明によれば、送酸ランスとは別個に
1本以上のスプラッシュランスを可動的に炉体に装備し
たので、炉内のスラグあるいは溶湯レベルが処理中に変
動する場合においても、スプラッシュランスを用いて2
次燃焼帯に効果的に熱媒体であるスラグ液滴を飛ばすこ
とにより2火燃焼効率OD比=0.4以上において高着
熱効率を得ることが可能になった。Table 1 Per 1 ton of Cri-containing pig iron [Effects of the invention] As described above, according to the present invention, one or more splash lances are movably installed in the furnace body separately from the oxygen supply lance. Even if the slag or molten metal level in the tank fluctuates during processing, a splash lance can be used to
By effectively blowing slag droplets as a heat medium into the secondary combustion zone, it has become possible to obtain high heat transfer efficiency at a two-fire combustion efficiency OD ratio of 0.4 or higher.
CO+CO2+ H2+H20 である。CO+CO2+ H2+H20 It is.
第1図は本発明の実施例の概略構成図、第2図は第1図
r−を線における断面図、第3図は他の実施例の概略構
成図である。
(1):炉体、(2):金属溶湯、(3):送酸ランス
、(51: スラグ、(10): スプラッシュランス
。FIG. 1 is a schematic configuration diagram of an embodiment of the present invention, FIG. 2 is a sectional view taken along the line r- in FIG. 1, and FIG. 3 is a schematic configuration diagram of another embodiment. (1): Furnace body, (2): Molten metal, (3): Oxidation lance, (51: Slag, (10): Splash lance.
Claims (1)
及び炭材を添加して鉱石の溶融還元を行うものにおいて
、前記送酸ランスとは別個に金属溶湯表面に存在するス
ラグの液滴を生成、飛散させるための1本以上のスプラ
ッシュランスを可動的に炉体に装備したことを特徴とす
るスプラッシュランスを有する溶解・製錬容器。In a method that melts and reduces ore by adding ore and carbonaceous material while spraying oxygen from an acid lance to the molten metal, droplets of slag existing on the surface of the molten metal are generated separately from the acid lance. A melting/smelting vessel having a splash lance, characterized in that the furnace body is movably equipped with one or more splash lances for splashing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25379385A JPS62116712A (en) | 1985-11-14 | 1985-11-14 | Melting and smelting vessel having splash lance |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25379385A JPS62116712A (en) | 1985-11-14 | 1985-11-14 | Melting and smelting vessel having splash lance |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62116712A true JPS62116712A (en) | 1987-05-28 |
Family
ID=17256223
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25379385A Pending JPS62116712A (en) | 1985-11-14 | 1985-11-14 | Melting and smelting vessel having splash lance |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62116712A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0605535A4 (en) * | 1991-09-20 | 1995-06-14 | Ausmelt Pty Ltd | Process for production of iron. |
KR100727729B1 (en) * | 1999-10-26 | 2007-06-13 | 테크놀라지칼 리소시스 피티와이. 리미티드. | Vessel for direct smelting process and direct smelting process thereby |
CN102719596A (en) * | 2012-03-29 | 2012-10-10 | 鞍钢股份有限公司 | Method for remaining slag at bottom of converter |
-
1985
- 1985-11-14 JP JP25379385A patent/JPS62116712A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0605535A4 (en) * | 1991-09-20 | 1995-06-14 | Ausmelt Pty Ltd | Process for production of iron. |
US5498277A (en) * | 1991-09-20 | 1996-03-12 | Ausmelt Limited | Process for production of iron |
KR100727729B1 (en) * | 1999-10-26 | 2007-06-13 | 테크놀라지칼 리소시스 피티와이. 리미티드. | Vessel for direct smelting process and direct smelting process thereby |
CN102719596A (en) * | 2012-03-29 | 2012-10-10 | 鞍钢股份有限公司 | Method for remaining slag at bottom of converter |
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