JPH08325621A - Production of high carbon molten iron from iron scrap - Google Patents
Production of high carbon molten iron from iron scrapInfo
- Publication number
- JPH08325621A JPH08325621A JP13311295A JP13311295A JPH08325621A JP H08325621 A JPH08325621 A JP H08325621A JP 13311295 A JP13311295 A JP 13311295A JP 13311295 A JP13311295 A JP 13311295A JP H08325621 A JPH08325621 A JP H08325621A
- Authority
- JP
- Japan
- Prior art keywords
- iron
- slag
- molten iron
- carbonaceous material
- 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.)
- Granted
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
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、上底吹転炉型の容器を
用いて屑鉄から、高炭素溶融鉄を製造する方法に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing high carbon molten iron from scrap iron by using an upper-bottom blow converter type container.
【０００２】[0002]
【従来の技術】近年、資源、環境問題からスクラップを
リサイクル使用して、効率的に溶融金属を製造すること
が技術課題となってきている。その金属スクラップの種
類は種々のものがあるが、発生量の多い屑鉄を用いて溶
融鉄を得る方法として、従来はほとんど電気炉で行われ
てきた。しかし、電気炉の場合は、屑鉄の溶解、精錬に
多くの電力を消費するため、わが国のように電力価格が
著しく高い国ではコストアップして好ましくない。そこ
で、電気炉によらずに経済的に屑鉄を溶解、精錬する方
法として、高吹酸能力を有する転炉の余剰生産能力を利
用して安価な炭材を用いた屑鉄の溶解、精錬方法が検討
されるようになってきた。2. Description of the Related Art In recent years, it has become a technical subject to efficiently produce molten metal by recycling scraps due to resource and environmental problems. There are various kinds of metal scraps, but as a method for obtaining molten iron by using scrap iron, which has a large amount of generation, conventionally, most of it has been carried out in an electric furnace. However, in the case of an electric furnace, a large amount of electric power is consumed for melting and refining scrap iron, so that it is not preferable in a country where the electric power price is extremely high, such as Japan. Therefore, as a method of economically melting and refining scrap iron without using an electric furnace, there is a method of melting and refining scrap iron using inexpensive carbonaceous materials by utilizing the surplus production capacity of a converter having a high blowing acid capacity. It has come to be considered.
【０００３】このような状況の中で、一般的には既存の
上底吹の複合吹錬転炉を利用することで設備費増を控え
るとともに、屑鉄と炭材を炉内に装入し、酸素ガスを上
吹して溶解、精錬する方法が提案されている。例えば特
開昭６０−１７４８１２号公報で、溶銑等の高炭素溶融
鉄の存在する転炉内に含鉄冷材、炭材、酸素を供給し、
含鉄冷材を高炭素溶融鉄中で溶解し高炭素溶融鉄を得る
第１工程と、上記高炭素溶融鉄を原料として別の転炉で
酸素吹錬し所要の温度、成分の溶鋼を得る第２工程より
なる転炉製鋼法が知られている。Under such circumstances, generally, the existing upper-bottom-blown composite smelting converter is used to suppress the increase in equipment cost, and scrap iron and carbonaceous materials are charged into the furnace. A method has been proposed in which oxygen gas is blown upward to dissolve and refine. For example, in JP-A-60-174812, an iron-containing cold material, carbonaceous material, and oxygen are supplied into a converter in which high-carbon molten iron such as hot metal exists.
The first step of melting the iron-containing cold material in the high-carbon molten iron to obtain the high-carbon molten iron, and the oxygen blowing of the high-carbon molten iron in another converter to obtain the molten steel of the required temperature and composition A converter steelmaking method comprising two steps is known.
【０００４】また、特開昭６２−７３９９７号公報で、
種湯の存在する溶解専用転炉に含鉄冷材、炭材、酸素を
供給して高炭素溶鉄を得、この溶鉄を原料として別の精
錬専用転炉において、上記精錬専用転炉での所要精錬量
と溶解専用転炉での所要種湯量の合計量の高炭素溶鉄を
得、上記溶解専用転炉から上記精錬専用転炉での所要精
錬量の高炭素溶鉄を１回の出湯にて酸素精錬に供する一
方、高炭素溶鉄の残部種湯量を溶解専用転炉に残して前
記含鉄冷材溶解のための種湯として使用することを特徴
とする転炉製鋼法が知られている。Further, in JP-A-62-73997,
High-carbon molten iron is obtained by supplying iron-containing cold material, carbonaceous material, and oxygen to a dedicated melting furnace where seed water is present, and this molten iron is used as a raw material in another dedicated refining furnace for the required refining in the above-mentioned dedicated refining furnace. Amount of high-carbon molten iron of the total amount of the required amount of seed hot water in the dedicated melting furnace and the required amount of refined high-carbon molten iron in the above-mentioned dedicated melting furnace is oxygen-refined in one tap. On the other hand, there is known a converter steel making method which is characterized in that the amount of the residual seed hot water of high carbon molten iron is left in a dedicated melting furnace for use as the seed hot water for melting the iron-containing cold material.
【０００５】上記のような、炭材を供給しつつ炉内のＣ
を酸素で燃焼させてその燃焼熱により屑鉄を溶解する方
法においては、できるだけＣを完全燃焼に近いところま
で燃焼させ、大きな燃焼熱を得て、かつその熱を効率よ
く屑鉄に伝えることが、少ない炭材・酸素原単位で効率
よく屑鉄を溶解するための鍵となる。すなわち、下式で
定義される二次燃焼率と着熱効率をできるだけ１００％
近くまで向上することが重要である。 二次燃焼率＝（排ガス中ＣＯ2 濃度）／（排ガス中ＣＯ濃度 ＋排ガス中ＣＯ2 濃度）×１００（％） 着熱効率＝〔１−｛排ガス顕熱のうちのメタル温度以上の分｝／ ｛二次燃焼発熱量（ＣＯ→ＣＯ2 分）｝〕×１００（％）As described above, while supplying the carbonaceous material, the C in the furnace is
In the method of burning waste iron with oxygen and melting the scrap iron by the heat of combustion, it is rare that C is burned as close to complete combustion as possible to obtain a large heat of combustion and the heat is efficiently transmitted to the scrap iron. It is the key to efficiently dissolve scrap iron with carbon materials and oxygen intensity. That is, the secondary combustion rate and heat transfer efficiency defined by
It is important to improve close. Secondary combustion rate = (CO 2 concentration in exhaust gas) / (CO concentration in exhaust gas + CO 2 concentration in exhaust gas) x 100 (%) Heat transfer efficiency = [1- {min of exhaust gas sensible heat above metal temperature} / {Secondary combustion calorific value (CO → CO 2 minutes)}] × 100 (%)
【０００６】しかるに、上記の方法では、着熱効率が９
０％を超えるような条件下での最大の二次燃焼率は高々
３０％程度であり、屑鉄を溶解するための炭材や酸素の
原単位が高く、上吹酸素の供給能力の上限から溶解時間
も長いという問題があった。また、上吹ランスの高さを
上昇させることで、空間で二次燃焼（ＣＯ→ＣＯ2 の燃
焼）を促進させ、二次燃焼を４０〜５０％程度まで高め
ることも可能ではあるが、その場合には、高温の二次燃
焼帯が上部にあるため着熱効率が低下し、転炉の炉肩付
近の耐火物が異常溶損して耐火物コストが大幅に増大す
るのが実状であった。However, in the above method, the heat transfer efficiency is 9
The maximum secondary combustion rate under conditions of more than 0% is at most about 30%, the carbonaceous material for dissolving scrap iron and the basic unit of oxygen are high, and it melts from the upper limit of the upper blowing oxygen supply capacity. There was a problem that it took a long time. Further, by increasing the height of the upper blowing lance, it is possible to promote secondary combustion (combustion of CO → CO 2 ) in the space and increase the secondary combustion to about 40 to 50%. In this case, since the high temperature secondary combustion zone is located in the upper part, the heat deposition efficiency is lowered, and the refractory in the vicinity of the shoulder of the converter is abnormally melted, resulting in a substantial increase in refractory cost.
【０００７】これらに対し、本出願人らは先に特願平７
−６３８３５号にて、転炉型の容器を用いて屑鉄を溶解
する新プロセスを提案し、その優位性を確認した。すな
わち、前記新プロセスの要旨とするところは、転炉型の
容器を用いて、上吹き吹酸をしながら炉内の炭材を燃焼
させつつ屑鉄を溶解するに際し、種湯が存在する容器に
屑鉄を装入し、炉内のスラグ量を炉内の溶融鉄１ｔ当た
り１００ｋｇ以上１０００ｋｇ以下として、酸素ジェッ
トによるスラグ凹み深さＬS と酸素ジェットが当たって
いない部分のスラグ厚みＬSOの比ＬS ／ＬSOが０．５〜
１の範囲内になるように、上吹きランス高さ、ランスの
ノズル形状および吹酸速度の１種または２種以上を調整
することを特徴とする屑鉄の溶解方法にある。この方法
により屑鉄溶解に必要な炭材および酸素の原単位を顕著
に低減することが可能となった。On the other hand, the present applicants previously filed Japanese Patent Application No.
In No. -63835, a new process for melting scrap iron using a converter type vessel was proposed, and its superiority was confirmed. That is, the gist of the new process is to use a converter-type vessel to melt the scrap iron while burning the carbonaceous material in the furnace while spraying top-blown acid, and Scrap iron is charged, and the amount of slag in the furnace is set to 100 kg or more and 1000 kg or less per 1 t of molten iron in the furnace, and the ratio L of the slag dent depth L S due to the oxygen jet to the slag thickness L SO not hit by the oxygen jet is L S / L SO is 0.5 ~
It is a method for melting scrap iron, characterized in that one or more kinds of the height of the upper blowing lance, the shape of the nozzle of the lance, and the velocity of blowing acid are adjusted so as to fall within the range of 1. By this method, it became possible to remarkably reduce the basic unit of carbonaceous material and oxygen required for melting scrap iron.
【０００８】[0008]
【発明が解決しようとする課題】上述した溶解方法を、
本出願人らは大型の上底吹転炉に適用すべく、試験を進
めていく中で、特願平７−６３８３５号の如き屑鉄の溶
解法は、屑鉄の溶解速度に比較して加炭速度が追従せ
ず、高炭素溶融鉄の安定的な製造が困難であることが判
明した。その結果、脱炭処理工程で熱源が不足するとい
う問題、また炭材やＦｅ−Ｓｉなどの昇熱材を用いた場
合には硫黄による溶融鉄の汚染や、スラグ量の増大、さ
らには終点濃度の的中率が低下するといった問題が顕在
化した。本発明者らは、この加炭遅れは転炉の大型化に
伴う溶融鉄と、スラグ中炭材の接触面積の低下が原因で
あると推定した。すなわち、屑鉄溶解量は体積（単位長
さの３乗）で増加するのに対し、溶融鉄と炭材が接触す
る面積（単位長さの２乗）は体積の増加分に見合うまで
には増加しないためと考えた。本発明はかかる問題点を
有利に解決したものであり、上底吹転炉型の容器炉にお
いて，屑鉄から高炭素溶融鉄を製造する方法を提供する
ものである。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
While the applicants are proceeding with the test so as to apply it to a large-scale top-and-bottom blowing converter, the method for melting scrap iron, such as Japanese Patent Application No. 7-63835, is used in comparison with the melting speed of scrap iron for carburizing. It was found that the speed did not follow and stable production of high carbon molten iron was difficult. As a result, there is a problem of insufficient heat source in the decarburization process, and when using a carbonaceous material or a heat-raising material such as Fe-Si, contamination of molten iron with sulfur, an increase in the amount of slag, and further an end point concentration. The problem that the hit rate of the target has decreased has become apparent. The present inventors presumed that this delay in carburization was caused by a decrease in the contact area between the molten iron and the carbonaceous material in the slag as the converter size increased. In other words, the amount of dissolved scrap iron increases with the volume (the cube of the unit length), whereas the area where the molten iron and the carbonaceous material contact (the square of the unit length) increases until the volume increases. I thought not to do it. The present invention advantageously solves such problems, and provides a method for producing high carbon molten iron from scrap iron in a container furnace of the upper and lower blown converter type.
【０００９】[0009]
【課題を解決するための手段】即ち、本発明の要旨とす
るところは、上底吹転炉型の容器を用いて、屑鉄から高
炭素溶融鉄を製造する方法において、種湯が存在する容
器に屑鉄を装入し、炉内のスラグ量を炉内の溶融鉄１ｔ
当たり１００ｋｇ以上１０００ｋｇ以下とし、該スラグ
内の炭材量をスラグ量の５％〜２００％に保ち、供給屑
鉄１ｔ当たり１０〜１２０ｋｇの炭材をキャリアーガス
とともに底吹きしながら、上吹酸素ジェットによるスラ
グ凹み深さＬS と酸素ジェットが当たっていない部分の
スラグ厚みＬSOの比ＬS ／ＬSOが０．５〜１の範囲内に
なるように、上吹きランス高さ、ランスのノズル形状お
よび吹酸速度の１種または２種以上を調整して吹酸しな
がら炉内の炭材を燃焼させて、屑鉄を溶解することを特
徴とする屑鉄から高炭素溶融鉄を製造する方法にある。That is, the gist of the present invention is to provide a method for producing high carbon molten iron from scrap iron using an upper-bottom blowing converter type vessel, in which seed water is present. Scrap iron was charged into the furnace, and the amount of slag in the furnace was adjusted to 1 t of molten iron in the furnace.
The amount of carbonaceous material in the slag is kept at 5% to 200% of the slag amount, and 10 to 120 kg of carbonaceous material per 1 ton of supplied scrap iron is blown with the carrier gas by the top blowing oxygen jet. The upper blowing lance height and the nozzle shape of the lance so that the ratio L S / L SO of the slag depression depth L S and the slag thickness L SO of the portion not hit by the oxygen jet is within the range of 0.5 to 1. And a method of producing high carbon molten iron from scrap iron, characterized in that one or more of the spraying acid velocity is adjusted and the carbonaceous material in the furnace is burned while spraying acid to dissolve scrap iron. .
【００１０】上述のＬS は（１）式により計算される。 ２．５ρg 〔（ｃＨC ）／Ｘ＋ＬS 〕2 ＝ρS ｇＬS ・・・・（１） ρg ：常温、常圧での酸素ガスの密度（＝１．４３ｋｇ
／ｍ3 ） ρs ：見掛けのスラグ密度（ｋｇ／ｍ3 ） ｃ ：常温、常圧での酸素ガス中の音速（＝３２６ｍ3
／ｓ） ＨC ：操業条件と同一ランスノズル形状、同一ランス二
次圧で噴出される常温でのジェットコア長（ノズル先端
から噴流中心流速が音速ｃとなるまでの距離）（ｍ） Ｘ ：ランスノズル先端から、酸素ジェットが当たって
いない部分のスラグ面までの鉛直距離（ｍ） ｇ ：重力加速度＝９．８（ｍ／ｓ2 ）The above-mentioned L S is calculated by the equation (1). 2.5 ρ g [(cH C ) / X + L S ] 2 = ρ S gL S ... (1) ρ g : Density of oxygen gas at normal temperature and pressure (= 1.43 kg)
/ M 3 ) ρ s : Apparent slag density (kg / m 3 ) c: Velocity of sound in oxygen gas at normal temperature and pressure (= 326 m 3
/ S) H C : Jet core length (distance from nozzle tip to jet velocity at sonic velocity c) at room temperature ejected with the same lance nozzle shape and the same lance secondary pressure as operating conditions (m) X: Vertical distance from the tip of the lance nozzle to the slag surface where the oxygen jet is not hit (m) g: Gravity acceleration = 9.8 (m / s 2 )
【００１１】[0011]
【数１】 [Equation 1]
【００１２】ＭP ：ランスノズルの設計マッハ数 ｄ ：ランスノズルのスロート径（ｍ） Ｐ ：ランスの操業二次圧（Ｐａ） ＰP ：ランスの設計二次圧（Ｐａ） また、本発明における高炭素溶融鉄とは炭素含有量が３
〜５％のものをいう。M P : Design Mach Number of Lance Nozzle d: Throat Diameter of Lance Nozzle (m) P: Lance Operation Secondary Pressure (Pa) P P : Lance Design Secondary Pressure (Pa) High-carbon molten iron has a carbon content of 3
~ 5%.
【００１３】[0013]
【作用】以下、本発明について図面に従って詳細に説明
する。図１は本発明に係わる屑鉄の溶解精錬を行う溶解
炉の概念図である。図１に示すように、上底吹転炉１は
耐火物２で内張りされており、酸素上吹ランス３を備え
ている。酸素上吹ランス３より酸素ガスを高炭素溶融鉄
４上の、炭材５を含んだ溶融スラグ６に向けて吹き付け
る。石炭やコークスなどの炭材７および屑鉄８を上方か
ら添加する。炉底にはノズル９を配置し微粉炭材１０を
底吹ガス１１をキャリアーにして、炉内に供給する。The present invention will be described in detail below with reference to the drawings. FIG. 1 is a conceptual diagram of a melting furnace for melting and refining scrap iron according to the present invention. As shown in FIG. 1, an upper bottom blowing converter 1 is lined with a refractory material 2 and is provided with an oxygen upper blowing lance 3. Oxygen gas is blown toward the molten slag 6 containing the carbonaceous material 5 on the high carbon molten iron 4 from the oxygen top blowing lance 3. Carbon material 7 such as coal and coke and scrap iron 8 are added from above. A nozzle 9 is arranged at the bottom of the furnace, and fine carbonaceous material 10 is supplied into the furnace by using a bottom blowing gas 11 as a carrier.
【００１４】このように上底吹転炉の上方から酸素上吹
ランスを通して吹き込まれるのは酸素ガスである。この
酸素は高濃度の酸素含有ガスであり、純酸素ガス、或い
は７０％以上の酸素を含む比較的純度の低い酸素ガス、
或いは純酸素ガスと空気、窒素のような希釈ガスの混合
物で、酸素濃度の７０〜１００％のものをいう。このよ
うな酸素ガスは溶融スラグ４の上から供給するものや、
斜め上方より吹いても良い。なお、複数の穴から酸素を
供給するときは一部は微粉炭バーナーを利用することも
可能である。屑鉄ならびに造滓材は主として上方より投
入される。屑鉄は、予熱されないもの、予熱されたもの
を連続的に投入ないしは間欠装入のいずれを組み合わせ
て、適宜分割して装入する。一方、造滓材は例えば、石
灰、硅砂、レンガ屑、高炉スラグ、転炉スラグが挙げら
れ、これらの組み合わせで塩基度を０．７〜２．２に制
御することが好ましい。炭材は上方添加、および底吹ノ
ズルからの微粉炭材の吹込を組み合わせて炉内に供給す
る。As described above, oxygen gas is blown from above the upper-bottom blowing converter through the oxygen upper-blowing lance. This oxygen is a high-concentration oxygen-containing gas, and is pure oxygen gas or oxygen gas with a relatively low purity containing 70% or more oxygen,
Alternatively, it means a mixture of pure oxygen gas and a diluting gas such as air and nitrogen, which has an oxygen concentration of 70 to 100%. Such oxygen gas is supplied from above the molten slag 4,
You may blow from diagonally above. When supplying oxygen from a plurality of holes, a pulverized coal burner can be partially used. Scrap iron and slag material are mainly charged from above. The scrap iron is not preheated, or the preheated one is continuously charged or intermittently charged, and is appropriately divided and charged. On the other hand, examples of the slag material include lime, silica sand, brick waste, blast furnace slag, and converter slag, and it is preferable to control the basicity to 0.7 to 2.2 by combining these. The carbonaceous material is fed into the furnace by a combination of upward addition and injection of fine carbonaceous material from the bottom blowing nozzle.
【００１５】そして、酸素ガスは炭材、溶融鉄中の炭素
および発生ＣＯなどの可燃ガス成分を燃焼させて発熱
し、屑鉄の溶解熱を供給する。一方、底吹ガスには溶融
物を攪拌する効果があり、伝熱進行に必要である。この
底吹ガスとしては、前述したように、Ｎ2 、ＣＯ2 、ア
ルゴン、炭化水素系ガスなどの１種ないしは２種以上の
混合ガスが用いられる。微粉炭材とともに炉内に吹き込
むキャリアーガスには、Ｎ2 、Ａｒなどの不活性ガスを
用いる。The oxygen gas burns the carbonaceous material, carbon in the molten iron and combustible gas components such as generated CO to generate heat, and supplies the heat of dissolution of scrap iron. On the other hand, the bottom blowing gas has the effect of stirring the melt and is necessary for the progress of heat transfer. As the bottom blowing gas, as described above, one kind or a mixed gas of two or more kinds such as N 2 , CO 2 , argon and hydrocarbon type gas is used. An inert gas such as N 2 or Ar is used as the carrier gas blown into the furnace together with the fine carbonaceous material.
【００１６】本発明は、一定量の溶融鉄が存在する転炉
に屑鉄を装入し、石炭やコークス等の炭材を供給しつ
つ、酸素の上吹きにより炉内のＣを燃焼させ、その燃焼
熱を利用して屑鉄を溶解する。この際、屑鉄の溶解速度
は主としてＣの移動律速であるため、屑鉄装入前に一定
量の溶融鉄すなわち種湯が存在しないと、固体Ｃが固体
屑鉄中に拡散していかなくてはならず、溶解速度が著し
く低下する。従って溶解速度を向上させるためには、予
め種湯を転炉内に残しておき、液体である種湯中のＣが
屑鉄に拡散するようにしておく必要がある。According to the present invention, scrap iron is charged into a converter in which a certain amount of molten iron is present, and while carbonaceous material such as coal and coke is supplied, C in the furnace is burned by top blowing oxygen, Uses heat of combustion to dissolve scrap iron. At this time, the rate of dissolution of scrap iron is mainly the rate-determining movement of C, so solid C must diffuse into solid scrap iron unless a certain amount of molten iron, that is, seed water, exists before charging scrap iron. However, the dissolution rate is significantly reduced. Therefore, in order to improve the dissolution rate, it is necessary to leave the seed hot water in the converter in advance so that C in the liquid seed hot water diffuses into the scrap iron.
【００１７】屑鉄溶解操業の際、先に提案した方法のよ
うに、炉内のスラグ量を炉内の溶融鉄１ｔ当たり１００
ｋｇ以上１０００ｋｇ以下とし、酸素ジェットによるス
ラグ凹み深さＬS と酸素ジェットが当たっていない部分
のスラグ厚みＬSOの比ＬS ／ＬSOが０．５〜１の範囲内
になるように、上吹きランス高さ、ランスのノズル形状
および吹酸速度を調整する。この条件下では、多量のス
ラグによって上吹酸素ジェットとバルク溶融鉄の接触が
防止でき、先に述べた二次燃焼率を高めることが可能に
なる。ここで、炉内のスラグ量やＬS ／ＬSOを限定した
のは、炉内のスラグ量が溶融鉄１ｔ当たり１００ｋｇ未
満の場合やＬS ／ＬSOが１．０超の場合には、酸素ジェ
ットがスラグを突き抜け、バルク溶融鉄に衝突して２Ｃ
＋Ｏ2 ＝２ＣＯの如く反応して二次燃焼率を低下させて
しまうためであり、ＬS ／ＬSOが０．５未満の場合には
９０％以上の着熱効率が達成できず、スラグ量が生成溶
融鉄１ｔ当たり１０００ｋｇを超えると、出銑時にスラ
グが炉口から溢れてきて所定の量を出銑できないためで
ある。In the scrap iron melting operation, the amount of slag in the furnace is set to 100 per 1 t of molten iron in the furnace, as in the method proposed above.
1 kg or more and 1000 kg or less so that the ratio L S / L SO of the slag dent depth L S due to the oxygen jet and the slag thickness L SO not hit by the oxygen jet falls within the range of 0.5 to 1. Adjust the blowing lance height, lance nozzle shape, and blowing acid velocity. Under this condition, the contact between the top-blown oxygen jet and the bulk molten iron can be prevented by the large amount of slag, and the secondary combustion rate described above can be increased. Here, the amount of slag in the furnace and L S / L SO are limited only when the amount of slag in the furnace is less than 100 kg per 1 t of molten iron, or when L S / L SO is more than 1.0. The oxygen jet penetrates the slag and collides with the bulk molten iron, resulting in 2C
This is because it reacts like + O 2 = 2CO to lower the secondary combustion rate, and when L S / L SO is less than 0.5, the heat deposition efficiency of 90% or more cannot be achieved, and the amount of slag increases. This is because when the amount of generated molten iron exceeds 1,000 kg, the slag overflows from the furnace port during tapping and a predetermined amount cannot be tapped.
【００１８】当該スラグ内の炭材量はスラグ量の５％〜
２００％に保つよう操業を行う。これは当該スラグ内の
炭材量がスラグ量の５％未満では、スラグの泡立ち（フ
ォーミング）が著しく、スラグが炉外に溢れ出るなどし
て、安定操業が困難になる。また当該スラグ内の炭材量
がスラグ量の２００％超では、炭材がスラグ内に均一に
存在することが困難で、スラグ上部に炭材が積み重なっ
た状態となり、炭材の燃焼で一旦発生したＣＯ2 が炭材
とＣＯ2 ＋Ｃ＝２ＣＯの如く反応して二次燃焼率が低下
し、好ましくない。また微粉炭材の底吹供給量は、供給
屑鉄１ｔ当たり１０〜１２０ｋｇとするが、１０ｋｇ未
満では屑鉄の溶解速度に対し加炭速度が追従せず、安定
的に高炭素溶融鉄を製造することが困難になる。一方１
２０ｋｇ超では、加炭、燃焼で消費されなかった炭材の
排ガス中に混入して飛散ロスが著しくなり、熱ロスなら
びに炭材原単位の上昇を招き好ましくない。The amount of carbonaceous material in the slag is 5% to 5% of the amount of slag.
Operate to maintain at 200%. This is because when the amount of carbonaceous material in the slag is less than 5% of the amount of slag, foaming (forming) of the slag is remarkable and the slag overflows to the outside of the furnace, which makes stable operation difficult. If the amount of carbonaceous material in the slag exceeds 200% of the amount of slag, it is difficult for the carbonaceous material to be present uniformly in the slag, and the carbonaceous material is piled up on the upper part of the slag and once generated by combustion of the carbonaceous material. and CO 2 is reduced carbonaceous material and CO 2 + C = 2CO reaction to post combustion ratio as was unfavorable. Further, the bottom blowing supply amount of the fine carbonaceous material is set to 10 to 120 kg per 1 ton of supplied scrap iron, but if it is less than 10 kg, the carburizing speed does not follow the dissolution rate of the scrap iron, and stable production of high carbon molten iron is possible. Becomes difficult. While 1
If it exceeds 20 kg, the carbonaceous material that has not been consumed by carburization and combustion is mixed in the exhaust gas, and the scattering loss becomes significant, resulting in heat loss and an increase in the carbonaceous material unit.
【００１９】[0019]
【実施例】溶融スラグ３５ｔと、該スラグ内に１６ｔの
炭材が浮遊している３００ｔ規模の転炉に高炉溶銑１５
０ｔを装入した。このときのスラグおよび溶融鉄の温度
は１４００℃、溶融鉄中の炭素濃度は４．５％であっ
た。上吹ランスからは３５０００Ｎｍ3 ／ｈの純酸素
を、炉底に設けた６本の底吹羽口からは、Ｎ2 ガスを４
５００Ｎｍ3 ／ｈ、酸素を３６００Ｎｍ3 ／ｈ、空気を
７００Ｎｍ3 ／ｈ、ＬＰＧを５００Ｎｍ3 ／ｈ、および
微粉炭材を２４ｔ／ｈで供給した。上方からは炭材を合
計９ｔ、また塩基度調整用に生石灰を合計４．５ｔ添加
した。微粉炭材ならびに、上方から添加する炭材には、
いずれも無煙炭（Ｔ−Ｃ：８１．５％）を用いた。屑鉄
は溶融鉄の温度が１３５０〜１４５０℃の範囲となるよ
うに供給速度を調整しながら炉内に装入し、合計１５０
ｔの屑鉄を溶解した。溶解期間中の各諸元を表１に示
す。EXAMPLE A molten slag 35t and a blast furnace hot metal 15 of a 300t scale converter in which 16t of carbonaceous material floats in the slag.
I loaded 0t. At this time, the temperatures of the slag and the molten iron were 1400 ° C., and the carbon concentration in the molten iron was 4.5%. 35,000 Nm 3 / h of pure oxygen was supplied from the top blowing lance, and N 2 gas of 4 was supplied from the six bottom blow holes installed in the furnace bottom.
500 Nm 3 / h, oxygen was 3600 Nm 3 / h, air was 700 Nm 3 / h, LPG was 500 Nm 3 / h, and fine carbonaceous material was supplied at 24 t / h. A total of 9 t of carbonaceous material and a total of 4.5 t of quicklime were added from above to adjust the basicity. For fine carbonaceous materials and carbonaceous materials added from above,
Both used anthracite (TC: 81.5%). Scrap iron was charged into the furnace while adjusting the feed rate so that the temperature of the molten iron was in the range of 1350 to 1450 ° C, and a total of 150
The scrap iron of t was melted. Table 1 shows each parameter during the dissolution period.
【００２０】[0020]
【表１】 [Table 1]
【００２１】比較例 用いた炉は実施例１と同一のものである。溶融スラグ３
５ｔと、該スラグ内に１６ｔの炭材が浮遊している３０
０ｔ規模の転炉に高炉溶銑１５０ｔを装入した。このと
きのスラグおよび溶融鉄の温度は１４２０℃、溶融鉄中
の炭素濃度は４．７％であった。上吹ランスからは３５
０００Ｎｍ3 ／ｈで純酸素を、炉底に設けた６本の底吹
ノズルからは、Ｎ2 ガスを４５００Ｎｍ3 ／ｈ、酸素を
３６００Ｎｍ3 ／ｈ、空気を７００Ｎｍ3 ／ｈで供給
し、底吹ノズルからの微粉炭材の吹込は行わなかった。
上方からは炭材を合計２０ｔ、また塩基度調整用に生石
灰を合計４．０ｔ添加した。上方から添加する炭材に
は、実施例と同様に無煙炭（Ｔ−Ｃ：８１．５％）を用
いた。屑鉄は溶融鉄の温度が１３５０〜１４５０℃の範
囲となるように供給速度を調整しながら炉内に装入し、
合計１５０ｔの屑鉄を溶解した。溶解期間中の各諸元を
表１に示す。この操業では、操業期間中に溶融鉄中の炭
素濃度の低下が認められ、溶解終了時点での炭素濃度は
２．８％であった。Comparative Example The furnace used is the same as in Example 1. Molten slag 3
5t and 16t of carbonaceous material suspended in the slag 30
150 tons of blast furnace hot metal was charged into a 0 ton scale converter. At this time, the temperatures of the slag and the molten iron were 1420 ° C., and the carbon concentration in the molten iron was 4.7%. 35 from Kamabuki Lance
000Nm 3 / h in pure oxygen from the six bottom blowing nozzle provided in the furnace bottom, and supplies N 2 gas 4500 nm 3 / h, the oxygen 3600 nm 3 / h, the air at 700 Nm 3 / h, bottom The pulverized carbonaceous material was not blown from the blowing nozzle.
From the upper side, a total of 20 t of carbonaceous material and a total of 4.0 t of lime were added for adjusting the basicity. As the carbonaceous material added from above, anthracite (TC: 81.5%) was used as in the example. Scrap iron was charged into the furnace while adjusting the feed rate so that the temperature of the molten iron was in the range of 1350 to 1450 ° C.
A total of 150 tons of scrap iron was melted. Table 1 shows each parameter during the dissolution period. In this operation, a decrease in the carbon concentration in the molten iron was observed during the operation period, and the carbon concentration at the end of melting was 2.8%.
【００２２】[0022]
【発明の効果】以上述べたように、本発明を実施するこ
とによって、屑鉄を溶解しつつ、安定して高炭素溶融鉄
を得ることが可能となった。As described above, by carrying out the present invention, it becomes possible to stably obtain high carbon molten iron while melting scrap iron.
【図１】本発明に係わる屑鉄溶解法に使用する反応容器
の概念図である。FIG. 1 is a conceptual diagram of a reaction vessel used in a scrap iron melting method according to the present invention.
1 上底吹転炉 2 耐火物 3 酸素上吹ランス 4 高炭素溶融鉄 5 炭材 6 溶融スラグ 7 炭材 8 屑鉄 9 底吹ノズル 1 0 微粉炭材 1 1 攪拌ガス 1 Top-bottom blow converter 2 Refractory 3 Oxygen top-blowing lance 4 High carbon molten iron 5 Carbon material 6 Molten slag 7 Carbon material 8 Scrap iron 9 Bottom blowing nozzle 1 0 Fine carbon material 1 1 Stirred gas
───────────────────────────────────────────────────── フロントページの続き (72)発明者 奥村 恭司 千葉県富津市新富20−１ 新日本製鐵株式 会社技術開発本部内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kyoji Okumura 20-1 Shintomi, Futtsu-shi, Chiba Nippon Steel Corp. Technology Development Division
Claims (1)
高炭素溶融鉄を製造する方法において、種湯が存在する
容器に屑鉄を装入し、炉内のスラグ量を炉内の溶融鉄１
ｔ当たり１００ｋｇ以上１０００ｋｇ以下とし、該スラ
グ内の炭材量をスラグ量の５％〜２００％に保ち、供給
屑鉄１ｔ当たり１０〜１２０ｋｇの炭材をキャリアーガ
スとともに底吹きしながら、上吹酸素ジェットによるス
ラグ凹み深さＬS と酸素ジェットが当たっていない部分
のスラグ厚みＬSOの比ＬS ／Ｌ SOが０．５〜１の範囲内
になるように、上吹きランス高さ、ランスのノズル形状
および吹酸速度の１種または２種以上を調整して吹酸し
ながら炉内の炭材を燃焼させて屑鉄を溶解することを特
徴とする屑鉄から高炭素溶融鉄を製造する方法。1. From scrap iron using an upper-bottom blow converter type container
Seed water is present in the method for producing high carbon molten iron
Charge scrap iron into the container and set the amount of slag in the furnace to the molten iron in the furnace 1
100 kg or more and 1000 kg or less per t
Supply the amount of carbonaceous material inside the slag at 5% to 200% of the slag amount
Carrier gas of 10 to 120 kg of carbonaceous material per ton of scrap iron
While blowing bottom with the spray,
Depth of lug LSAnd the part not hit by the oxygen jet
Slag thickness LSORatio ofS/ L SOWithin the range of 0.5 to 1
Top blowing lance height, lance nozzle shape
And one or more of the blowing acid rates are adjusted
While melting the scrap iron by burning the carbonaceous material in the furnace
A method for producing high carbon molten iron from scrap iron.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13311295A JP3286114B2 (en) | 1995-05-31 | 1995-05-31 | Method for producing high carbon molten iron from scrap iron |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13311295A JP3286114B2 (en) | 1995-05-31 | 1995-05-31 | Method for producing high carbon molten iron from scrap iron |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH08325621A true JPH08325621A (en) | 1996-12-10 |
| JP3286114B2 JP3286114B2 (en) | 2002-05-27 |
Family
ID=15097096
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13311295A Expired - Fee Related JP3286114B2 (en) | 1995-05-31 | 1995-05-31 | Method for producing high carbon molten iron from scrap iron |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3286114B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20200057498A (en) * | 2018-11-16 | 2020-05-26 | 주식회사 포스코 | Manufacturing method for molten iron and apparatus thereof |
| KR20200057499A (en) * | 2018-11-16 | 2020-05-26 | 주식회사 포스코 | Manufacturing method for molten iron and apparatus thereof |
| CN114096685A (en) * | 2019-07-22 | 2022-02-25 | 杰富意钢铁株式会社 | Method for dephosphorizing molten iron |
-
1995
- 1995-05-31 JP JP13311295A patent/JP3286114B2/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20200057498A (en) * | 2018-11-16 | 2020-05-26 | 주식회사 포스코 | Manufacturing method for molten iron and apparatus thereof |
| KR20200057499A (en) * | 2018-11-16 | 2020-05-26 | 주식회사 포스코 | Manufacturing method for molten iron and apparatus thereof |
| CN114096685A (en) * | 2019-07-22 | 2022-02-25 | 杰富意钢铁株式会社 | Method for dephosphorizing molten iron |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3286114B2 (en) | 2002-05-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP2380995B1 (en) | Smelting vessel, steel making plant and steel production method | |
| AU676203B2 (en) | A method for intensifying the reactions in metallurgical reaction vessels | |
| US8845779B2 (en) | Process for producing molten iron | |
| CN107419051B (en) | Promote the smelting process of converter scrap melting using gasification dephosphorized slag | |
| US4324583A (en) | Supersonic injection of oxygen in cupolas | |
| JP2004503681A (en) | Direct smelting method and equipment | |
| JP3286114B2 (en) | Method for producing high carbon molten iron from scrap iron | |
| US5084093A (en) | Method for manufacturing molten pig iron | |
| JP3290844B2 (en) | Scrap iron dissolution method | |
| JP2983087B2 (en) | Operation method of smelting reduction | |
| JP7136390B1 (en) | Molten iron smelting method | |
| WO2022234762A1 (en) | Electric furnace and steelmaking method | |
| JPS61195909A (en) | Method for melting iron scrap in converter | |
| JP2002003917A (en) | Method for supplying oxygen in vertical melting furnace | |
| Stone | Oxygen in Steelmaking | |
| JPH08209219A (en) | Method for smelting stainless steel | |
| JPH01195211A (en) | Method for melting and reducing iron oxide | |
| JPH03111507A (en) | Method and apparatus for producing molten ferrous alloy | |
| JPH08283818A (en) | Production of low sulfur and high carbon molten iron from scrap | |
| JPH07207325A (en) | Method for melting scrap using carbonaceous material as fuel | |
| JPH0379709A (en) | Slag bath type smelting reduction producing apparatus for molten ferrous alloy and method thereof | |
| JPS61227119A (en) | Manufacture of steel in converter using cold material containing iron as principal starting material | |
| JPH032306A (en) | Production of molten pig iron combined with recovery of rare metal | |
| JPS6338506A (en) | Adding method for powdery carbon material into smelting reduction furnace | |
| JPH09143522A (en) | Method for melting iron scrap at high speed |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20020226 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080308 Year of fee payment: 6 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090308 Year of fee payment: 7 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090308 Year of fee payment: 7 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100308 Year of fee payment: 8 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110308 Year of fee payment: 9 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120308 Year of fee payment: 10 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130308 Year of fee payment: 11 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130308 Year of fee payment: 11 |
|
| S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130308 Year of fee payment: 11 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130308 Year of fee payment: 11 |
|
| S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130308 Year of fee payment: 11 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140308 Year of fee payment: 12 |
|
| LAPS | Cancellation because of no payment of annual fees |