JPH01195224A - Operating method for molten iron gutter type smelting reduction iron manufacture - Google Patents

Operating method for molten iron gutter type smelting reduction iron manufacture

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Publication number
JPH01195224A
JPH01195224A JP2016688A JP2016688A JPH01195224A JP H01195224 A JPH01195224 A JP H01195224A JP 2016688 A JP2016688 A JP 2016688A JP 2016688 A JP2016688 A JP 2016688A JP H01195224 A JPH01195224 A JP H01195224A
Authority
JP
Japan
Prior art keywords
iron
hot metal
smelting reduction
gas
reduction
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
Application number
JP2016688A
Other languages
Japanese (ja)
Inventor
Mitsuhiro Fukuda
光弘 福田
Isao Kobayashi
勲 小林
Yoshimichi Takenaka
竹中 芳通
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP2016688A priority Critical patent/JPH01195224A/en
Publication of JPH01195224A publication Critical patent/JPH01195224A/en
Pending legal-status Critical Current

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  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To reduce iron manufacturing cost by recovering CO-contg. gas produced from a smelting reduction iron manufacturing device and utilizing it for fuel or reduction. CONSTITUTION:An iron manufacturing raw material, carbon material and oxygen are fed to the molten iron flowing through a molten iron gutter and the iron oxide component incorporated in the above-mentioned raw material is melted and reduced. CO-contg. gas produced from this process is recovered and it is utilized as valuable gas for fuel or reduction after removing dust.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、銑鉄製造装置から溶銑樋を通して流出してく
る溶銑を熱源とし、且っ該溶銑中の炭素を還元剤として
活用すると共に、更に炭材及び酸素を補給することによ
って鉄鉱石、予備還元鉄鉱石、スクラップ等の製鉄原料
を溶融還元して製鉄を行なう方法の改良に関し、殊に溶
融還元工程で生成する大量のCO含有ガスを有価ガスと
して有効利用することにより、工場操業の経済性を向上
することのできる方法に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention uses hot metal flowing out from a pig iron production device through a hot metal trough as a heat source, and utilizes carbon in the hot metal as a reducing agent. Regarding the improvement of a method for producing iron by melting and reducing iron ore, pre-reduced iron ore, scrap, and other raw materials for steelmaking by supplementing carbonaceous material and oxygen, it is particularly important to reduce the amount of CO-containing gas produced in the melting and reduction process. The present invention relates to a method that can improve the economic efficiency of factory operations by effectively utilizing the gas as a gas.

[従来の技術] 製鉄手段は、高炉法に代表される間接製鉄法敏溶融還元
法に代表される直接製鉄法に大別され、現在は連続操業
が可能で大量生産に適した高炉法が主流となっている。
[Conventional technology] Steel manufacturing methods are broadly divided into indirect iron manufacturing methods, represented by the blast furnace method, and direct iron manufacturing methods, represented by the rapid smelting reduction method.Currently, the blast furnace method, which allows continuous operation and is suitable for mass production, is the mainstream. It becomes.

ところが高炉法は、厖大な建設費と維持管理費を要する
という問題に加えて、竪型移動床反応を利用する方法で
あるから、操業効率や操業安定性を高めるためには、還
元剤として作用するコークス及び鉄源たる鉄鉱石を適当
な大きさと圧潰強度を持ったものに調整しなければなら
ず、装入原料の調整に多大な手数と費用がかかる。
However, in addition to the problem of requiring enormous construction and maintenance costs, the blast furnace method uses a vertical moving bed reaction, so in order to improve operational efficiency and stability, it is necessary to use a method that acts as a reducing agent. The coke to be used and iron ore, which is the iron source, must be adjusted to have appropriate size and crushing strength, and it takes a great deal of effort and cost to adjust the charging raw materials.

これに対し溶融還元製鉄法では高炉はど大きな設備が必
要とされず、また鉄鉱石等の製鉄原料を溶融状態で還元
する方法であるから、比較的低品位の石炭でも、また粉
状の鉄鉱石等でも支障なく使用することができ、更には
固体−気体間の還元反応を主体とする高炉法に比べて反
応速度および反応効率が高いといった利点を有している
ところから、最近各社で検討されている。
On the other hand, the smelting reduction method does not require large blast furnace equipment, and since it is a method that reduces iron ore and other raw materials for iron making in a molten state, it can be used even with relatively low-grade coal or powdered iron ore. It can be used with stones, etc. without any problems, and it has the advantage of higher reaction rate and reaction efficiency than the blast furnace method, which mainly involves a reduction reaction between solids and gases. has been done.

〔発明が解決しようとする課題] 溶融還元製鉄法は、使用する炉の形式によって分類され
、代表的なものとしては、回転炉を用いる方法、転炉型
鉄浴炉を用いる方法およびコークス充填型竪型炉を用い
る方法の3f!が挙げられるが、これらの方法における
共通の問題は、出湯・出滓の連続化ができず生産性が低
いということである。即ちこれらの方法はいずれもバッ
チ式で溶融還元を行ない、出銑・出滓はたとえば1〜2
時間周期で間欠的に行なわれるので、高炉を用いる連続
法に比べると出銑・出滓作業やそれらの後処理作業が面
倒であるばかりでなく、後処理炉はその都度冷却される
ので熱効率も低く、また生産性を高めるにはある程度の
量の溶銑および溶滓を炉内に貯留しておかなければなら
ないので、高炉設備はどではないにしてもかなり大型の
設備が必要となる。
[Problems to be Solved by the Invention] Smelting reduction ironmaking methods are classified according to the type of furnace used. Typical methods include methods using a rotary furnace, methods using a converter type iron bath furnace, and coke-filled methods. 3f of method using vertical furnace! However, a common problem with these methods is that they cannot continuously tap the hot water and tap the slag, resulting in low productivity. In other words, in all of these methods, melting and reduction is carried out in a batch manner, and the tapping and slag are produced in 1 to 2 batches, for example.
Since the operations are carried out intermittently over time, compared to the continuous method using a blast furnace, not only are the tapping and slag tapping operations and their post-processing operations cumbersome, but the post-processing furnace is cooled each time, resulting in lower thermal efficiency. Moreover, in order to increase productivity, a certain amount of hot metal and molten slag must be stored in the furnace, so a fairly large blast furnace equipment is required.

本発明者らはこの様な状況のもとで、設備費および運転
経費のいずれの面からしても経済的であり、しかも連続
化が可能で生産性の高い製鉄法の開発を期して研究を行
なっているが、その成果の1つとして、高炉やキュポラ
或は溶融還元製鉄装置等の銑鉄製造装置(以下単に銑鉄
製造装置という)における溶銑樋を流れる溶銑を熱源と
し、且つ該溶銑中の炭素を還元剤として製鉄原料の溶融
還元を行なう方法を開発し、先に特許出願を済ませた(
特願昭62−186400号二未公開)。
Under these circumstances, the present inventors conducted research with the aim of developing a steel manufacturing method that is economical in terms of both equipment costs and operating costs, and that is continuous and highly productive. One of the results of this research is that the heat source is the hot metal flowing through the hot metal gutter in pig iron manufacturing equipment such as blast furnaces, cupolas, or smelting reduction iron making equipment (hereinafter simply referred to as pig iron manufacturing equipment), and the We have developed a method for melting and reducing raw materials for steelmaking using carbon as a reducing agent, and have already filed a patent application (
(Japanese Patent Application No. 186400/1982, unpublished).

即ちこの方法は、溶銑樋を流れる溶銑中に製鉄原料を吹
込み、溶銑の保有熱を熱源として利用すると共に溶銑中
に含まれる炭素を主たる還元剤として活用し、更に熱源
及び還元剤の不足を補うために炭材と燃焼用酸素を供給
しつつ、溶銑中に製鉄原料を吹込んで溶融還元を行なう
方法であって、従来の溶融還元製鉄法に比べると、■連
続操業が可能で生産性が高い、 ■設備を著しく小規模化できる、 ■溶銑中に含まれる珪素やマンガンも還元剤として活用
されるので還元剤の消費量が少なく、且つ溶銑の保有熱
も有効に活用されるから熱効率が高い、 ■溶融還元により生成した溶銑および副生ずる溶滓は下
流側で効率良く分離・排出されるので、後処理性が良い
、 といった多くの特徴を有している。
In other words, this method injects ironmaking raw materials into hot metal flowing through hot metal sluices, uses the retained heat of the hot metal as a heat source, and utilizes the carbon contained in the hot metal as the main reducing agent, further eliminating the shortage of heat sources and reducing agents. This method involves injecting ironmaking raw materials into hot metal to perform smelting reduction while supplying carbonaceous materials and combustion oxygen to supplement the process. ■Equipment can be significantly downsized; ■Silicon and manganese contained in the hot metal are also used as reducing agents, so the consumption of reducing agents is small, and the heat retained in the hot metal is also effectively used, increasing thermal efficiency. It has many features such as: (1) hot metal produced by melt reduction and by-product slag are efficiently separated and discharged on the downstream side, so post-processing is good.

ところで上記の溶融還元反応は還元性7囲気下で行なわ
れるものであり、具体的には、炭材の燃焼によって生成
するcoを主体とする還元性ガスを利用している。この
還元性ガスは、還元反応に寄与して還元度が若干低下し
ているものの依然としてかなりの還元性を有しているが
、前記先願発明ではこの還元性ガスを更に有効利用する
ことについては格別の考慮は払われていなかった。
By the way, the above-mentioned melt reduction reaction is carried out under a reducing atmosphere, and specifically, a reducing gas mainly composed of co produced by combustion of carbonaceous material is used. Although this reducing gas contributes to the reduction reaction and the degree of reduction is slightly reduced, it still has considerable reducing properties, but the prior invention does not discuss how to use this reducing gas more effectively. No special consideration was given.

本発明は上記の様な状況に着目してなされたものであっ
て、その目的は、溶銑樋式の溶融還元製鉄工程で副生ず
る大量の還元性ガスを、有価ガスとして更に利用できる
様にし、製鉄工場全体の操業コストを低減しようとする
ものである。
The present invention has been made in view of the above-mentioned situation, and its purpose is to make it possible to further utilize a large amount of reducing gas, which is produced as a by-product in the molten iron trough type smelting reduction iron manufacturing process, as a valuable gas. The aim is to reduce the operating costs of the entire steel mill.

[課題を解決するための手段] 上記の課題を解決することのできた本発明に係る製鉄操
業法の構成は、銑鉄製造装置の溶銑樋を流れる溶銑に、
製鉄原料、炭材及び酸素を供給し、該製鉄原料中の酸化
鉄成分を溶融還元すると共に、ここで回収されるCO含
有ガスは、除塵後右価ガスとして利用するところに要旨
を有するものである。
[Means for Solving the Problems] The structure of the iron manufacturing operation method according to the present invention that can solve the above problems is that the hot metal flowing through the hot metal gutter of the pig iron manufacturing equipment,
The purpose is to supply ironmaking raw materials, carbonaceous materials, and oxygen, and melt and reduce the iron oxide components in the ironmaking raw materials, and the CO-containing gas recovered here is used as a valuable gas after dust removal. be.

[作用] 本発明の特徴は、前述の如き銑鉄製造装置に設けられる
溶銑樋上で溶融還元製鉄を行なうに当たり、主に炭材の
燃焼によって生成する還元性ガスを有価ガスとして有効
利用するところに存在する。
[Function] A feature of the present invention is that reducing gas produced mainly by combustion of carbonaceous material is effectively utilized as a valuable gas when performing smelting reduction ironmaking on a hot metal sluice provided in a pig iron manufacturing apparatus as described above. do.

たとえば第1図は、本発明が適用される溶融還元製鉄設
備を例示する概略縦断面説明図、第2図は排ガス利用シ
ステムを含めた本発明操業法の実施例を示す概略フロー
図である。
For example, FIG. 1 is a schematic vertical cross-sectional explanatory diagram illustrating a smelting reduction iron manufacturing facility to which the present invention is applied, and FIG. 2 is a schematic flow diagram illustrating an embodiment of the operating method of the present invention including an exhaust gas utilization system.

まず第1図において、lは溶銑樋の途中に設けられる溶
融還元製鉄設備、2は該設備1の上方を覆い、熱と排ガ
スの放散を防止するための蓋体、3は排滓樋、4は潜り
堰、5は越流基、6は製鉄原料吹込み管、7は酸素吹込
み管、8は炭材吹込み管、9は排ガスダクト、10は溶
銑鍋、Mは溶銑、Sは溶滓(スラグ)、Cは炭材を夫々
示している。
First, in Fig. 1, 1 is a smelting reduction ironmaking equipment installed in the middle of a hot metal trough, 2 is a lid that covers the upper part of the equipment 1 and prevents the dissipation of heat and exhaust gas, 3 is a slag trough, 4 5 is a submerged weir, 5 is an overflow base, 6 is a steelmaking raw material blowing pipe, 7 is an oxygen blowing pipe, 8 is a carbon material blowing pipe, 9 is an exhaust gas duct, 10 is a hot metal pot, M is hot metal, S is molten iron. Slag and C indicate carbonaceous material, respectively.

高炉(第2図の符号11)等の銑鉄製造装置から溶銑樋
を通して排出される溶銑および溶滓のうち比重の小さい
溶滓は、図示する溶融還元製鉄設備1に至るまでの上流
側適所で分離除去される。
Of the hot metal and molten slag that are discharged from the pig iron manufacturing equipment such as the blast furnace (numeral 11 in Figure 2) through the hot metal gutter, the molten slag with a lower specific gravity is separated at a suitable location on the upstream side up to the smelting reduction steelmaking equipment 1 shown in the figure. removed.

そしてその下流適所の溶銑樋にやや深めの滞留部を設け
て図示する様な溶融還元製鉄設備1を形成する。即ちこ
の溶融還元製鉄設備1は、放熱防止と排ガス拡散防止を
兼ねた蓋体2に、製鉄原料吹込み管6、酸素吹込み管7
、炭材吹込み管8および排ガスダクト9が取付けられて
なり、製鉄原料吹込み管6からは鉄鉱石、予備還元鉱石
、スクラップ等の鉄分含有原料と生石灰等の副原料を適
当な比率で溶銑Mの深部へ吹込むと共に、炭材吹込み管
8からは粉粒状の炭材Cを吹込み、同時に酸素吹込み管
7から酸素(または空気)を吹込む。溶銑M内へ吹込ま
れた製鉄原料は溶銑Mの保有熱および炭材の燃焼熱によ
って溶融し、且つ製鉄原料中の酸化鉄成分は、溶銑M中
に多量含まれけている旦や吹込み炭材Cおよび該炭材C
の燃焼によって生成する一酸化炭素の作用を受けて還元
される。そして生成した鉄分は溶銑M中へ取り込まれ、
一方比重の小さいスラグ成分Sは溶銑Mの表面に浮上し
た状態で順次流下し、排滓樋3から分離・排出される。
Then, a slightly deeper retention section is provided in the molten metal trough at a suitable location downstream, thereby forming the smelting reduction iron making equipment 1 as shown in the figure. That is, this smelting reduction iron manufacturing equipment 1 includes a lid body 2 that serves both to prevent heat radiation and exhaust gas diffusion, a steel manufacturing raw material blowing pipe 6, and an oxygen blowing pipe 7.
, a carbonaceous material blowing pipe 8 and an exhaust gas duct 9 are installed, and from the steelmaking raw material blowing pipe 6, iron-containing raw materials such as iron ore, pre-reduced ore, scrap, etc. and auxiliary raw materials such as quicklime are injected into hot metal in an appropriate ratio. At the same time, powdery carbonaceous material C is blown in from the carbonaceous material blowing pipe 8, and at the same time, oxygen (or air) is blown in from the oxygen blowing pipe 7. The iron making raw material injected into the hot metal M is melted by the retained heat of the hot metal M and the combustion heat of the carbonaceous material, and the iron oxide component in the iron making raw material is mixed with the iron oxide contained in a large amount in the hot metal M and the blown coal. Material C and the carbon material C
is reduced by the action of carbon monoxide produced by combustion. The generated iron is then taken into the hot metal M.
On the other hand, the slag component S having a small specific gravity flows down one after another while floating on the surface of the hot metal M, and is separated and discharged from the slag drain 3.

尚第1図では、製鉄原料、炭材および酸素(空気)を別
々に吹込む様にした例を示したが、これら3者を1つの
吹込み管から混合状態で同時に吹込んだり、あるいは任
意の組合せで適当に混合して吹込むこともでき、更には
溶銑流の流れ方向に沿って複数箇所から製鉄原料や炭材
等を吹込み、複数箇所で還元反応を進めることもできる
。また炭材Cは溶銑内へ吹込むのが最も効果的であるが
、場合によっては溶銑流の上方に散布し湯面の波立ちに
よって溶銑内へ混入させることもできる。
Although Fig. 1 shows an example in which raw materials for steelmaking, carbonaceous material, and oxygen (air) are blown in separately, these three may be blown in in a mixed state from one blowing pipe, or they can be blown in at any time. It is also possible to properly mix and inject a combination of these, and furthermore, it is also possible to inject ironmaking raw materials, carbonaceous materials, etc. from multiple locations along the flow direction of the hot metal flow, and to proceed with the reduction reaction at multiple locations. Although it is most effective to blow the carbonaceous material C into the hot metal, in some cases it can also be dispersed above the hot metal flow and mixed into the hot metal by the ripples on the hot metal surface.

ところで上記の様な溶融還元製鉄工程では、COを50
〜90%程度含有する還元性ガスが大量に生成するが、
本発明ではこのCO含有ガスを排ガスダクト9を通して
吸引し、たとえば第2図に示す様なフローに従い有価ガ
スとして有効利用できる様にしている。
By the way, in the above-mentioned smelting reduction steelmaking process, 50% of CO is
A large amount of reducing gas containing ~90% is produced,
In the present invention, this CO-containing gas is sucked through the exhaust gas duct 9 and can be effectively used as a valuable gas according to the flow shown in FIG. 2, for example.

即ち溶融還元製鉄設備1の排ガスダクト9から抜き出さ
れた高温のCO含有ガスは、熱交換器12に通すことに
より製鉄原料の予熱に利用した後、クーラー13で冷却
し、たとえばベンチュリースクラバー14あるいはサイ
クロン15と電気集塵機16を組合せた除塵設備等を通
すことによって、微粉炭や微粉鉱石等よりなる粉塵を除
去し、燃焼性および還元性を持ったクリーンガスとして
、当該製鉄設備もしくはその関連設備等で有価ガスとし
て活用する。尚図示例は、除塵されたco含有ガスを昇
圧ブロワ−17に通して昇圧し、還元エネルギーを更に
高めた状態で、たとえば[I]発電用ボイラーの燃料ガ
ス、[II ]高炉シャフト下部から吹込まれる還元ガ
ス、[III ]高炉羽口部から吹込む還元ガス、ある
いは[rVl高炉用熱風炉の燃料ガス等として活用でき
る様にしている。即ち本発明で回収されるco含有ガス
は、燃料ガスあるいは還元性ガスとして様々の用途に有
効に活用することができるが、第2図に示した如く当該
溶融還元製鉄設備あるいはその関連設備内で有効利用す
る様にすれば、設備全体としてのランニングコスト低減
に寄与することができ、ひいては製銑コストの低下に反
映させることができる。同様の趣旨で、たとえば製鉄原
料として予備還元鉱石を使用する様な場合は、鉄鉱石の
予備還元に前記CO含有ガスを利用することも有効であ
る。また高炉設備においては、炉頂部から大量のCO含
有ガスが排出されるが、このガスも還元ガスあるいは燃
料として有用なものであり、且つ多量の粉塵を含んでい
るので、冷却・除塵・昇圧機能を備えた排ガス処理設備
19で排ガス回収を行なうのが通例である。そこで、た
とえば第2図にも示す如く溶融還元排ガスを当該高炉排
ガスラインに合流させて排ガス処理設備19へ送り、高
炉排ガスと共に冷却・除塵・昇圧等を行なう様にすれば
、溶融還元排ガス専用の排ガス処理設備を省略すること
ができ、設備費並びに運転経費を軽減することができる
ので好ましい。
That is, the high-temperature CO-containing gas extracted from the exhaust gas duct 9 of the smelting reduction steelmaking equipment 1 is passed through the heat exchanger 12 to be used for preheating the steelmaking raw material, and then cooled by the cooler 13 and then passed through the venturi scrubber 14 or By passing through dust removal equipment that combines a cyclone 15 and an electrostatic precipitator 16, dust made of pulverized coal, pulverized ore, etc. is removed, and the gas is converted into clean gas with combustibility and reducing properties, such as the steel manufacturing equipment or its related equipment. It is used as valuable gas. In the illustrated example, the dust-removed co-containing gas is passed through the booster blower 17 to increase the pressure and further increase the reduction energy. [III] Reducing gas blown in from the blast furnace tuyere, [rVl] It can be used as a fuel gas for a hot blast furnace for blast furnaces, etc. In other words, the co-containing gas recovered in the present invention can be effectively used for various purposes as a fuel gas or reducing gas, but as shown in Fig. If used effectively, it can contribute to reducing the running cost of the equipment as a whole, which in turn can be reflected in a reduction in ironmaking costs. To the same effect, when pre-reduced ore is used as a raw material for iron ore, it is also effective to use the CO-containing gas for pre-reduction of iron ore. In addition, in blast furnace equipment, a large amount of CO-containing gas is discharged from the top of the furnace, but this gas is also useful as a reducing gas or fuel, and also contains a large amount of dust, so it is necessary to perform cooling, dust removal, and pressurization functions. It is customary to collect exhaust gas in an exhaust gas treatment facility 19 equipped with a. Therefore, as shown in Fig. 2, for example, if the smelting reduction exhaust gas is combined with the blast furnace exhaust gas line and sent to the exhaust gas treatment equipment 19, where it is cooled, dust removed, pressurized, etc. together with the blast furnace exhaust gas, it is possible to This is preferable because exhaust gas treatment equipment can be omitted and equipment costs and operating costs can be reduced.

[実施例] 8産溶銑量が8000トンの高炉設備の溶銑樋に、第1
図に示した様な溶融還元製鉄装置を設け、酸化鉄成分と
してヘマタイト鉱石またはスクラップを用いて下記第1
表に示す条件で溶融還元製鉄を行ない、約1400)−
ン/日(増産率17.5%)の溶銑増産操業を行なった
[Example] In the hot metal gutter of a blast furnace facility with a production capacity of 8,000 tons, the first
A smelting reduction iron manufacturing equipment as shown in the figure is installed, and hematite ore or scrap is used as the iron oxide component.
Smelting reduction iron production was carried out under the conditions shown in the table, and approximately 1400)
The company carried out increased hot metal production operations at a rate of 17.5% per day (17.5% increase in production rate).

第   1 ゛  表 その結果、何れの場合も、溶銑温度の調整、排滓処理の
円滑化(副原料の調整等)および排ガス回収設備の安定
化等を含めて2日間の準備期間で定常操業状態に達する
ことが確認された。
Table 1 As a result, in all cases, steady operation was achieved within a two-day preparation period, including adjustment of hot metal temperature, smooth treatment of tailings (adjustment of auxiliary raw materials, etc.), and stabilization of exhaust gas recovery equipment. It was confirmed that it reached.

これに対し高炉操業条件を変えることにより製銑量を8
産8000トンから9400トン(増産量1400)−
ン/日)に増産しようとした場合は、高炉への吹込み送
風量を約20%増加させる必要があり、過去の実績では
送風量を2%程度増加する毎に操炉状態を安定化させて
(通常1週間乃至10日程度を必要とする)段階的に送
風量を増加していかねばならず、上述の増産量1400
トン/日を達成する為には約3か月を要するものと考え
られ、こうした傾向は製銑量を減産する場合についても
同様である。
On the other hand, by changing the blast furnace operating conditions, the amount of iron production can be increased by 8.
Production from 8,000 tons to 9,400 tons (increase in production by 1,400 tons)
In order to increase production by approximately 2% per day), it is necessary to increase the amount of air blown into the blast furnace by approximately 20%, and past results indicate that the furnace operating condition must be stabilized every time the amount of air blown is increased by approximately 2%. The amount of air blown must be increased in stages (usually taking about 1 week to 10 days), and the above-mentioned increased production volume of 1400
It is thought that it will take about 3 months to achieve this rate per ton/day, and this trend is the same when reducing the amount of iron production.

即ち本発明の溶銑樋式溶融還元製鉄操業法によれば、高
炉操業条件を変更する方法に比べて、掻く短い準備期間
で製銑の増産もしくは減産を行なうことができ、目標製
銑量に応じて生産計画を柔軟に対応させることが可能と
なる。
That is, according to the hot metal gutter type smelting reduction ironmaking operation method of the present invention, compared to the method of changing the blast furnace operating conditions, it is possible to increase or decrease the production of pig iron in a much shorter preparation period, and it is possible to increase or decrease the production of pig iron in accordance with the target pig iron production amount. This makes it possible to flexibly adapt production plans.

また、前記第1表に示す増産法を実施する際に溶融還元
製鉄設備から排出されるCO含有ガスを、当該製鉄工場
に既設の発電用ボイラーの燃料としてLPGや重油の一
部と置換する方式で有効利用し、それに伴なう燃料費の
低減を加味した製銑コストを求め、通常の高炉製銑法に
おける製銑コストを1としたときの製銑コスト指数を算
出した。
In addition, when implementing the production increase method shown in Table 1 above, CO-containing gas discharged from smelting reduction steelmaking equipment is replaced with a portion of LPG or heavy oil as fuel for the existing power generation boiler in the steelmaking factory. The pig iron making cost was determined by taking into consideration the reduction in fuel cost that accompanies the effective utilization of iron, and the pig iron making cost index was calculated when the pig iron making cost in the normal blast furnace pig iron making method is set to 1.

結果は第3図に示す通りであり、製鉄原料としてスクラ
ップを用いた場合は、スクラップ自体の単価が高く且つ
CO含有ガスの生成量も比較的少ないので製銑コストは
むしろ高くなったが、ヘマタイト鉱石を使用した場合は
、通常の高炉法を採用した場合の約8割の費用で銑鉄を
増産し得ることが分かる。
The results are as shown in Figure 3. When scrap was used as a raw material for steelmaking, the unit price of scrap itself was high and the amount of CO-containing gas produced was relatively small, so the ironmaking cost was rather high. It can be seen that when ore is used, pig iron production can be increased at about 80% of the cost when using the normal blast furnace method.

[発明の効果] 本発明は以上の様に構成されており、製銑量の増産・減
産が容易で溶銑生産計画の自由度が高く、しかも溶融還
元製鉄設備で副生ずるCO含有ガスを燃料ガスあるいは
還元性ガスとして有効利用することにより、製銑コスト
の低減に反映し得ることになった。
[Effects of the Invention] The present invention is configured as described above, and it is easy to increase or decrease production of pig iron, and the degree of freedom in hot metal production planning is high.Moreover, CO-containing gas by-produced in smelting reduction ironmaking equipment is used as a fuel gas. Alternatively, by effectively using it as a reducing gas, it has become possible to reduce ironmaking costs.

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

第1図は溶銑樋式溶融還元製鉄設備を例示する概略縦断
面図、第2図は本発明の実施例を示す概略フロー図、第
3図は本発明法および従来法を採用したときの製銑コス
ト指数を対比して示すグラフである。 1・・・溶融還元製鉄設備 2・・・蓋体      3・・・排滓樋4・・・潜り
堰     5・・・越流堰6・・・製鉄原料吹込み管 7・・・酸素吹込み管  8・・・炭材吹込み管9・・
・排ガスダクト  10・・・溶銑鍋11・・・高炉 
     12・・・熱交換器13・・・クーラー 14・・・ベンチュリースクラバー 15・・・サイクロン分離器 16・・・電気集塵機   17・・・昇圧ブロアー1
8・・・加熱炉     19・・・排ガス処理設備第
3図
Fig. 1 is a schematic vertical cross-sectional view illustrating hot metal trough type smelting reduction ironmaking equipment, Fig. 2 is a schematic flow diagram showing an embodiment of the present invention, and Fig. 3 is a schematic longitudinal sectional view illustrating a hot metal gutter type smelting reduction iron manufacturing equipment. It is a graph showing a comparison of pig iron cost indexes. 1... Smelting reduction iron manufacturing equipment 2... Lid body 3... Slag gutter 4... Submerged weir 5... Overflow weir 6... Steel manufacturing raw material blowing pipe 7... Oxygen injection Pipe 8... Carbon material injection pipe 9...
・Exhaust gas duct 10...Hot metal pot 11...Blast furnace
12... Heat exchanger 13... Cooler 14... Venturi scrubber 15... Cyclone separator 16... Electrostatic precipitator 17... Boosting blower 1
8... Heating furnace 19... Exhaust gas treatment equipment Figure 3

Claims (1)

【特許請求の範囲】[Claims] (1)銑鉄製造装置の溶銑樋を流れる溶銑に、製鉄原料
、炭材及び酸素を供給し、該製鉄原料中の酸化鉄成分を
溶融還元すると共に、ここで回収されるCO含有ガスは
、除塵後有価ガスとして利用することを特徴とする溶銑
樋式溶融還元製鉄操業法。
(1) Iron-making raw materials, carbonaceous materials, and oxygen are supplied to the hot metal flowing through the hot-metal gutter of a pig iron production equipment, and the iron oxide component in the iron-making raw materials is melted and reduced, and the CO-containing gas recovered here is removed from dust. A hot metal trough type smelting reduction ironmaking operation method characterized by using the hot metal as post-valuable gas.
JP2016688A 1988-01-29 1988-01-29 Operating method for molten iron gutter type smelting reduction iron manufacture Pending JPH01195224A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2016688A JPH01195224A (en) 1988-01-29 1988-01-29 Operating method for molten iron gutter type smelting reduction iron manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2016688A JPH01195224A (en) 1988-01-29 1988-01-29 Operating method for molten iron gutter type smelting reduction iron manufacture

Publications (1)

Publication Number Publication Date
JPH01195224A true JPH01195224A (en) 1989-08-07

Family

ID=12019578

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2016688A Pending JPH01195224A (en) 1988-01-29 1988-01-29 Operating method for molten iron gutter type smelting reduction iron manufacture

Country Status (1)

Country Link
JP (1) JPH01195224A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004518020A (en) * 2000-05-15 2004-06-17 ヴォエスト・アルピーネ・インデュストリーアンラーゲンバウ・ゲーエムベーハー・ウント・コ Method and apparatus for producing pig iron or fluid primary iron from a charge containing iron ore

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004518020A (en) * 2000-05-15 2004-06-17 ヴォエスト・アルピーネ・インデュストリーアンラーゲンバウ・ゲーエムベーハー・ウント・コ Method and apparatus for producing pig iron or fluid primary iron from a charge containing iron ore

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