JP2679188B2 - Iron bath melt reduction ironmaking method - Google Patents

Iron bath melt reduction ironmaking method

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Publication number
JP2679188B2
JP2679188B2 JP30893888A JP30893888A JP2679188B2 JP 2679188 B2 JP2679188 B2 JP 2679188B2 JP 30893888 A JP30893888 A JP 30893888A JP 30893888 A JP30893888 A JP 30893888A JP 2679188 B2 JP2679188 B2 JP 2679188B2
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JP
Japan
Prior art keywords
coal
furnace
smelting reduction
iron bath
water
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 - Fee Related
Application number
JP30893888A
Other languages
Japanese (ja)
Other versions
JPH02156007A (en
Inventor
克博 岩崎
仁 川田
治良 田辺
正弘 川上
謙二 高橋
正廣 室屋
Original Assignee
日本鋼管株式会社
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Publication date
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Priority to JP30893888A priority Critical patent/JP2679188B2/en
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は鉄鉱石の溶融還元において、燃料として装入
される石炭の歩留を向上させるための方法に関する。
Description: TECHNICAL FIELD The present invention relates to a method for improving the yield of coal charged as a fuel in the smelting reduction of iron ore.

〔従来の技術〕[Conventional technology]

転炉型溶融還元炉を用いた鉄溶融還元において、炉内
に鉄鉱石、石炭等の原料を装入する方法として、原料を
炉上部から重力落下させる、所謂上置き法と、原料をノ
ズルにより溶湯中に吹き込むインジエクシヨン法とがあ
る。
In iron smelting reduction using a converter-type smelting reduction furnace, as a method of charging raw materials such as iron ore and coal into the furnace, the raw material is gravity dropped from the upper part of the furnace, a so-called top-down method, and the raw material by a nozzle There is an injection method that blows into the molten metal.

このうちインジエクシヨン法は、原料が直接溶湯中に
吹き込まれるため歩留良く反応するという利点がある
が、次のような欠点がある。
Among them, the infusion method has an advantage that the raw material is directly blown into the molten metal and thus the reaction is performed with good yield, but has the following drawbacks.

原料の粉砕処理が必要であり、製造コストが高い。The raw material needs to be crushed and the manufacturing cost is high.

特に炭材に関しては、炭塵爆発の危険があり、防爆対
策が必要である。このため設備コストが高くつく。
Especially for carbonaceous materials, there is a danger of coal dust explosion, and explosion-proof measures are necessary. Therefore, the equipment cost is high.

原料の供給設備が摩耗し易く、設備コストが高くな
る。
The raw material supply equipment is easily worn and the equipment cost increases.

これに対し、上置き法は原料の事前処理が必要なく、
また設備的な面でもインジエクシヨン法のような問題は
ない。
On the other hand, the superposition method does not require pretreatment of raw materials,
In terms of equipment, there is no problem like the infusion method.

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

しかし、この上置き法では、原料、特に燃料である石
炭の細粒が炉内から排出されるガスとともに炉外に飛散
するため、炭材の歩留が非常に悪いという大きな問題が
ある。本発明者等が検討したところによれば、このよう
に上置き法において石炭の歩留が悪いのは、急激な昇熱
による石炭の熱割れによるものである。石炭は一般炭で
約30%程度の揮発分を有しているが、溶融還元炉内は非
常な高温(1400℃以上)であるため、上置きの装入され
た石炭は急激に昇熱し、これに伴つて揮発分が急激にガ
ス化し、熱割れが生じる。そして、この熱割れにより生
じた細粒の一部が排ガスとともに炉外に排出されるもの
である。
However, in this superposition method, raw materials, particularly fine particles of coal, which is a fuel, are scattered outside the furnace together with the gas discharged from the furnace, so that there is a big problem that the yield of the carbonaceous material is very poor. According to the studies made by the present inventors, the poor yield of coal in the above-mentioned superposition method is due to thermal cracking of coal due to rapid heat rise. Coal is steam coal and has a volatile content of about 30%, but since the temperature inside the smelting reduction furnace is extremely high (1400 ° C or higher), the top-loaded coal rapidly heats up, Along with this, volatile components are rapidly gasified and thermal cracking occurs. Then, some of the fine particles generated by the thermal cracking are discharged outside the furnace together with the exhaust gas.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者らはこのような問題に鑑み、石炭の歩留向上
を目的として検討を重ねたものであり、その結果、石炭
中の水分含有量を従来考えられている範囲よりも高目の
ある範囲に調整することにより、熱割れを抑制し、石炭
原単位を効果的に低減させ得ることを見い出した。
In view of such problems, the present inventors have made repeated studies for the purpose of improving the yield of coal, and as a result, the water content in coal is higher than the conventionally considered range. It has been found that the thermal cracking can be suppressed and the coal unit consumption can be effectively reduced by adjusting the range.

従来、炭材として装入される石炭に水分が含まれる
と、その蒸発潜熱によつて石炭原単位が増大すると一般
に考えられ、このため石炭を天日等により乾燥させ、水
分を3%以下にして使用するというのが常識とされてい
た。これに対し、本発明では、石炭の水分含有量をこれ
よりも高い範囲に調整して使用するものである。
Conventionally, it is generally considered that when the coal charged as carbonaceous material contains water, the latent heat of vaporization increases the basic unit of coal. Therefore, the coal is dried by sun or the like to reduce the water content to 3% or less. It was common sense to use it. On the other hand, in the present invention, the water content of coal is adjusted to a range higher than this and used.

すなわち本発明は、炭材たる石炭の一部または全部を
炉上部のシユートを通じ上置き装入して行われる鉄浴式
溶融還元製鉄法において、炭材として4〜8wt%の水分
を含む石炭を使用するようにしたことをその特徴とす
る。
That is, the present invention is an iron bath type smelting reduction ironing method carried out by placing a part or all of coal, which is a carbonaceous material, through a shout at the upper part of a furnace, and using coal containing 4 to 8 wt% of water as the carbonaceous material. Its feature is that it is used.

〔作用〕[Action]

第1図は鉄浴式溶融還元操業の一例を示すもので、炉
内の溶銑に対し、底吹き羽口(2)や横吹羽口(1)か
らは撹拌ガスが、また、上吹きランス(3)からは酸素
が吹込まれ、炭材たる石炭は鉄鉱石とともに炉上部から
上置き装入される。
FIG. 1 shows an example of an iron bath smelting reduction operation, in which the stirring gas from the bottom blowing tuyeres (2) and side blowing tuyeres (1) and the top blowing lance ( Oxygen is blown in from 3), and coal, which is a carbonaceous material, is charged from above the furnace together with iron ore.

このような溶融還元操業における石炭の飛散は、上述
したように高温の炉内での急激な昇温に起因し、この昇
熱速度が大きくなるほど炉上部での石炭の熱割れは多く
なる。
Such coal scattering in the smelting reduction operation is caused by the rapid temperature rise in the high temperature furnace as described above, and the higher the heating rate, the more thermal cracking of the coal in the upper part of the furnace.

従来考えられているように、石炭中の水分の上昇はそ
の蒸発潜熱を増加させ、この面では石炭原単位を上昇さ
せる要因となる。これに対し本発明者らは、石炭中の水
分の蒸発潜熱は石炭の昇温を抑制することによつて熱割
れを抑える作用をし、その面では石炭原単位を低下させ
る要因となること、そして、ある水分含有量の範囲で
は、上記石炭原単位上昇要因があるにもかかわらず、そ
の石炭原単位低下要因により石炭原単位が最も低くなる
ことを見い出した。
As has been conventionally considered, an increase in water content in coal increases its latent heat of vaporization, which is a factor for increasing the unit consumption of coal. On the other hand, the inventors of the present invention, latent heat of vaporization of water in coal acts to suppress thermal cracking by suppressing the temperature rise of coal, and in that respect, it becomes a factor that reduces the coal basic unit, Then, it was found that, in the range of a certain water content, the coal basic unit becomes the lowest due to the coal basic unit decreasing factor in spite of the above-mentioned coal basic unit increasing factor.

第2図は石炭中の水分が石炭原単位に及ぼす影響を調
べたもので、図中(1)は水分蒸発潜熱による石炭原単
位上昇分、(2)は石炭の昇温抑制によつて熱割れが抑
えられ、石炭飛散が減少したことによる石炭原単位低下
分である。そして、実線((1)+(2))が(1)の
上昇分と(2)と低下分を相殺して得られた実際の石炭
原単位であり、水分含有量4〜8wt%の範囲において最
も低い石炭原単位が得られている。その効果は、水分0
%をベースにするとほぼ−40Kg/t程度にもなる。
Fig. 2 shows the effect of water content in coal on the basic unit of coal. In the figure, (1) is the amount of increase in the basic unit of coal due to the latent heat of evaporation of water, and (2) is the heat generated by suppressing the temperature rise of coal. This is the amount of decrease in coal intensity due to the suppression of cracking and the decrease in coal scattering. The solid line ((1) + (2)) is the actual coal intensity obtained by offsetting the increase in (1), the decrease in (2), and the decrease in water, and the water content is in the range of 4-8 wt%. Has the lowest coal intensity. The effect is 0 water
Based on%, it will be about -40 Kg / t.

なお、炭材として使用される石炭は普通篩により粒度
を選択したもの(例えば8〜22mm)が用いられるが、篩
分機器は大量処理・工業生産用のものであるため、篩に
かけたとしても8mm以下の粒径のものが通常10%程度含
まれている。そして、本発明のように水分が4〜8wt%
に調整された石炭を使用すると、上記のようにもとから
含まれている微粒の石炭も粗粒表面に付着水を介して付
着したまま炉内に装入され、この結果、炉口より飛散す
ることなくスラグ/メタル層に到達し、反応することに
なる。これに対し、十分に乾燥した石炭を用いる場合に
は、微粒は当初粗粒表面に付着しているものの、付着水
がほとんどないため装入時の炉内ガスとの接触により微
粒が粗粒表面から容易に離れ、飛散してしまう。このよ
うに本発明によれば、装入石炭中に当初から含まれる石
炭自体の飛散も抑えることができる効果がある。
It should be noted that the coal used as the carbonaceous material usually has a particle size selected by a sieve (for example, 8 to 22 mm), but since the sieving equipment is for large-scale processing / industrial production, even if it is sieved Usually, about 10% of particles with a particle size of 8 mm or less are included. And, as in the present invention, the water content is 4 to 8 wt%
When the coal adjusted to the above is used, the fine-grained coal originally contained in the above is also charged into the furnace while still adhering to the coarse-grained surface via the adhered water, and as a result, it is scattered from the furnace mouth. Without reaching, it will reach the slag / metal layer and react. On the other hand, when using sufficiently dried coal, fine particles initially adhere to the surface of the coarse particles, but since there is almost no adhered water, the fine particles will not contact the coarse gas surface during charging. Easily separates from and scatters. As described above, according to the present invention, there is an effect that it is possible to suppress the scattering of the coal itself which is initially contained in the charged coal.

〔実 施 例〕〔Example〕

第1図に示すような転炉型溶融還元炉(5Ton炉)を用
い、炭材として種々の水分含有量の石炭を使用して溶融
還元を実施し、石炭飛散率および石炭原単位を調べた。
その結果を操業条件とともに第1表に示す。
Using a converter-type smelting reduction furnace (5Ton furnace) as shown in Fig. 1, smelting reduction was carried out using coal with various water contents as carbonaceous materials, and the coal scattering rate and coal basic unit were investigated. .
The results are shown in Table 1 together with the operating conditions.

〔発明の効果〕 以上述べた本発明によれば、上置き装入された石炭の
熱割れとこの熱割れによる石炭の飛散を抑えることがで
き、加えて、装入石炭中に当初から不可避的に含まれて
いる微粒石炭の飛散も抑えることができ、これらにより
溶融還元操業における石炭原単位を効果的に低減させる
ことができる。
[Effects of the Invention] According to the present invention described above, it is possible to suppress thermal cracking of coal placed on top and scattering of coal due to this thermal cracking, and in addition, inevitably from the beginning during charging coal. It is also possible to suppress the scattering of fine coal contained in, and by these, it is possible to effectively reduce the coal basic unit in the smelting reduction operation.

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

第1図は溶融還元操業の一例を示す説明図である。第2
図は溶融還元で使用される石炭の水分含有量と石炭原単
位との関係を示すものである。
FIG. 1 is an explanatory view showing an example of the smelting reduction operation. Second
The figure shows the relationship between the water content of coal used in smelting reduction and the coal basic unit.

フロントページの続き (72)発明者 川上 正弘 東京都千代田区丸の内1丁目1番2号 日本鋼管株式会社内 (72)発明者 高橋 謙二 東京都千代田区丸の内1丁目1番2号 日本鋼管株式会社内 (72)発明者 室屋 正廣 東京都千代田区丸の内1丁目1番2号 日本鋼管株式会社内 (56)参考文献 特開 昭62−228413(JP,A) 特開 昭63−60217(JP,A)Front page continuation (72) Inventor Masahiro Kawakami Marunouchi 1-2-2, Nihon Koube Co., Ltd. (72) Inventor Kenji Takahashi Marunouchi 1-2-2 Nihon Koube Co., Ltd. (72) Inventor Masahiro Muroya 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Inside Nippon Kokan Co., Ltd. (56) References JP 62-228413 (JP, A) JP 63-60217 (JP, A) )

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】炭材たる石炭の一部または全部を炉上部の
シユートを通じ上置き装入して行われる鉄浴式溶融還元
製鉄法において、炭材として4〜8wt%の水分を含む石
炭を使用することを特徴とする鉄浴式溶融還元製鉄法。
1. An iron bath type smelting reduction ironing method carried out by placing a part or all of coal, which is a carbonaceous material, through a shout at the top of a furnace, and using coal containing 4 to 8 wt% of water as the carbonaceous material. Iron bath smelting reduction iron making method characterized by being used.
JP30893888A 1988-12-08 1988-12-08 Iron bath melt reduction ironmaking method Expired - Fee Related JP2679188B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30893888A JP2679188B2 (en) 1988-12-08 1988-12-08 Iron bath melt reduction ironmaking method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30893888A JP2679188B2 (en) 1988-12-08 1988-12-08 Iron bath melt reduction ironmaking method

Publications (2)

Publication Number Publication Date
JPH02156007A JPH02156007A (en) 1990-06-15
JP2679188B2 true JP2679188B2 (en) 1997-11-19

Family

ID=17987073

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30893888A Expired - Fee Related JP2679188B2 (en) 1988-12-08 1988-12-08 Iron bath melt reduction ironmaking method

Country Status (1)

Country Link
JP (1) JP2679188B2 (en)

Also Published As

Publication number Publication date
JPH02156007A (en) 1990-06-15

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