JPS62228406A - Operating method for melt reduction furnace - Google Patents
Operating method for melt reduction furnaceInfo
- Publication number
- JPS62228406A JPS62228406A JP7089886A JP7089886A JPS62228406A JP S62228406 A JPS62228406 A JP S62228406A JP 7089886 A JP7089886 A JP 7089886A JP 7089886 A JP7089886 A JP 7089886A JP S62228406 A JPS62228406 A JP S62228406A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- furnace
- reduction furnace
- melt reduction
- iron
- 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
- 238000011017 operating method Methods 0.000 title 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 47
- 239000007789 gas Substances 0.000 claims abstract description 35
- 229910052742 iron Inorganic materials 0.000 claims abstract description 22
- 239000000446 fuel Substances 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 11
- 239000000295 fuel oil Substances 0.000 claims abstract description 10
- 239000002893 slag Substances 0.000 claims abstract description 6
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000001301 oxygen Substances 0.000 claims abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 4
- 238000003723 Smelting Methods 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 10
- 239000003245 coal Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 238000002844 melting Methods 0.000 abstract description 6
- 230000008018 melting Effects 0.000 abstract description 6
- 239000011269 tar Substances 0.000 abstract description 2
- 239000000155 melt Substances 0.000 abstract 6
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 abstract 2
- 239000003638 chemical reducing agent Substances 0.000 abstract 2
- 235000012255 calcium oxide Nutrition 0.000 abstract 1
- 239000000292 calcium oxide Substances 0.000 abstract 1
- 239000002737 fuel gas Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000007790 solid phase Substances 0.000 abstract 1
- 239000002641 tar oil Substances 0.000 abstract 1
- 238000006722 reduction reaction Methods 0.000 description 23
- 229910000805 Pig iron Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は鉄鉱石等を溶融還元して銑鉄を得るための溶融
還元法に於いてのガス製造コントロールに関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to gas production control in a smelting reduction method for obtaining pig iron by smelting and reducing iron ore and the like.
(従来の技術)
近年高炉法等塊コークスや焼結鉱を用いて銑鉄を製造す
る方法に代わり、生鉱石や粉鉱石を粉石炭等の炭材と共
に鉄浴炉に吹き込んで直接溶鉄を得る溶融還元法が開発
されている(特開昭60−145307号等)、この方
法では鉄浴を得ると同時に炭材からガスを得られること
も出来るのであるが、しかし現在の段階ではガスの発生
を有効に利用してないのみならず、ガスの発生を有効に
利用すると共に鉄浴を維持を図ることの両者を効果的に
バランスさせて利用する技術はなかった。(Conventional technology) In recent years, instead of the blast furnace method, which uses lump coke and sintered ore to produce pig iron, raw ore and powdered ore are blown into an iron bath furnace together with carbonaceous materials such as powdered coal to directly produce molten iron. A reduction method has been developed (Japanese Unexamined Patent Publication No. 145307/1983), which makes it possible to obtain an iron bath and at the same time obtain gas from the carbonaceous material. Not only has it not been used effectively, but there has been no technology for effectively balancing the use of gas generation and maintaining the iron bath.
(発明が解決しようとする問題点)
従来製鉄業に於いて製鉄と共にガスの発生も他の工程等
とのからみより重要な掻業であり溶融還元法において、
あらゆる条件でガスの発生を出来るようにしておくこと
が重要であり、ガス発生を容易に行えるようにし、ガス
の発生と溶鉄を得ること或いは溶鉄の維持を必要に応じ
て円滑に行い得るようにした溶融還元炉の操業法を提供
することを目的としたものである。(Problems to be solved by the invention) Conventionally, in the steel industry, gas generation as well as iron production is a more important work than other processes, and in the smelting reduction method,
It is important to be able to generate gas under all conditions, so that gas generation can be performed easily, and gas generation and obtaining or maintaining molten iron can be performed smoothly as necessary. The purpose of this study is to provide a method for operating a smelting reduction furnace.
(問題点を解決するための手段)
本発明は鉄鉱石等を予備還元して炭材、酸素、造滓剤等
と共に、鉄浴中に吹き込む溶融還元法に於いて、昼間な
どガスの需要の高い時は溶融還元炉に石炭の他重油、タ
ール等の液体燃料も吹き込んでガスを多量に発生させ、
系外に出すことによりガス発生炉としての役割を成さし
め、ガスの需要の低い時は炭材の吹き込み量を浴鉄製造
に必要な量にバランスさせることにより鉄製造炉となら
しめることを特徴とする溶融還元炉の操業法である。(Means for Solving the Problems) The present invention is applicable to the smelting reduction method in which iron ore, etc. is pre-reduced and blown into an iron bath together with carbonaceous materials, oxygen, slag-forming agents, etc. When the temperature is high, in addition to coal, liquid fuels such as heavy oil and tar are injected into the smelting reduction furnace to generate a large amount of gas.
By taking it out of the system, it can function as a gas generating furnace, and when the demand for gas is low, it can be used as an iron manufacturing furnace by balancing the amount of carbon material injected to the amount required for bath iron manufacturing. This is a distinctive method of operating a melting reduction furnace.
(作用)
本発明は、溶融還元炉に石炭の他重油、タール等の液体
燃料を溶融還元炉に吹き込むと、溶融還元炉の溶融還元
反応を低下させガスを大量に発生することになる。この
時液体燃料を用いていることより、ノズルやランスが摩
耗することが無いので長期間ガス発生炉として使用させ
ることが出来る。(Function) In the present invention, when a liquid fuel such as heavy oil or tar in addition to coal is blown into the smelting reduction furnace, the smelting reduction reaction of the smelting reduction furnace is reduced and a large amount of gas is generated. Since liquid fuel is used at this time, the nozzle and lance do not wear out, so it can be used as a gas generating furnace for a long period of time.
更に重油、タールから得られるガスはH2やNH1多く
カロリーが高い為、使用価値の高いガスを提供出来る他
、溶融還元炉内で石炭を使用し発生する様な灰によるス
ラグの発生の防止を図ることが出来、炉の操業も容易に
行える。Furthermore, gas obtained from heavy oil and tar has a high caloric content due to its high H2 and NH1 content, so it is possible to provide a gas with high utility value, and also to prevent the generation of slag due to ash, which is generated when coal is used in a smelting reduction furnace. The furnace can be operated easily.
(実施例)
以下一般的な溶融11元法の工程に基づき説明する。溶
融還元炉に通常の溶融還元反応を行う場合には、還元鉄
などの主原耕を及び炭材、石炭粉又造滓剤等を鉄浴又は
スラグ浴に吹き込み溶融還元を行うものである。今溶融
還元炉をガス発生炉として使用する場合の操業について
一例を示すと、溶融還元炉内に一定の鉄浴が発生したの
ちに、溶融還元炉に炭材の他重油、タール等の液体燃料
を吹き込むと、液体燃料ば鉄浴により加熱されガスを発
生ずる。(Example) A description will be given below based on the steps of a general melting 11-element method. When carrying out a normal smelting reduction reaction in a smelting reduction furnace, smelting and reduction is carried out by blowing main raw material such as reduced iron, carbonaceous material, coal powder, slag forming agent, etc. into an iron bath or a slag bath. To give an example of the operation when a smelting reduction furnace is used as a gas generating furnace, after a certain amount of iron bath is generated in the smelting reduction furnace, liquid fuel such as carbonaceous material, heavy oil, tar, etc. When injected, the liquid fuel is heated by the iron bath and gas is generated.
(発明の効果)
本発明によれば溶融還元炉に石炭の他重油、タール等の
液体燃料を熔融還元炉に吹き込むことにより、78融還
元炉の溶融還元反応を低下させガスの発生を大量に増大
することが可能であり、ガスの需要の高い時はガスを系
外に出すことによりガス発生炉としての役割を果たすこ
とが出来る。この時液体燃料を用いていることより、ノ
ズルやランスが摩耗することが舞いので長期間ガス発生
炉として使用させることが出来る。又液体燃料或いは石
炭等の吹き込みを止めれば、溶融還元の操業が行え作業
効率が良い。更に重油、タール等の液体燃料を使用した
場合には重油、タールを溶融還元炉のノズルやランスか
ら溶融還元炉内に装入する為に炭材の如く粉末にする必
要がなく、しかも重油、タールから得られるガスはカロ
リーが高く使用価値の高いガスを提供出来る他、溶融1
7元炉内で石炭を使用し発生する様な灰によるスラグの
発生も防止を図ることが出来、通常の溶融還元の操業に
変更する場合も容易になる等価れた効果を有するもので
ある。(Effects of the Invention) According to the present invention, by injecting liquid fuel such as heavy oil or tar in addition to coal into the smelting reduction furnace, the smelting reduction reaction of the 78 smelting reduction furnace is reduced and gas generation is increased in large quantities. When the demand for gas is high, it can serve as a gas generating furnace by releasing the gas outside the system. Since liquid fuel is used at this time, the nozzle and lance are less likely to wear out, so it can be used as a gas generating furnace for a long period of time. Furthermore, if the injection of liquid fuel, coal, etc. is stopped, melting and reduction operations can be performed, resulting in good work efficiency. Furthermore, when liquid fuel such as heavy oil or tar is used, there is no need to turn the heavy oil or tar into powder like carbonaceous material in order to charge it into the melting reduction furnace through the nozzle or lance of the melting reduction furnace. Gas obtained from tar has a high calorific value and can provide gas with high utility value.
It is possible to prevent the generation of slag due to ash, which is generated when coal is used in a seven-head furnace, and it has an equivalent effect that makes it easy to change to normal smelting reduction operation.
Claims (1)
鉄浴中に吹き込む溶融還元法に於いて、昼間などガスの
需要の高い時は溶融還元炉に石炭の他重油、タール等の
液体燃料も吹き込んでガスを多量に発生させ、系外に出
すことによりガス発生炉としての役割を成さしめ、ガス
の需要の低い時は炭材の吹き込み量を溶鉄製造に必要な
量にバランスさせることにより鉄製造炉とならしめるこ
とを特徴とする、溶融還元炉の操業法。Preliminary reduction of iron ore, etc., along with carbonaceous material, oxygen, slag forming agent, etc.
In the smelting reduction method where gas is injected into the iron bath, during the daytime and other times when the demand for gas is high, in addition to coal, liquid fuels such as heavy oil and tar are injected into the smelting reduction furnace to generate a large amount of gas, which is then discharged from the system. The smelting reduction furnace is characterized in that it functions as a gas generating furnace, and when the demand for gas is low, it can function as an iron manufacturing furnace by balancing the amount of carbon material injected with the amount necessary for manufacturing molten iron. How to operate a furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7089886A JPS62228406A (en) | 1986-03-31 | 1986-03-31 | Operating method for melt reduction furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7089886A JPS62228406A (en) | 1986-03-31 | 1986-03-31 | Operating method for melt reduction furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62228406A true JPS62228406A (en) | 1987-10-07 |
Family
ID=13444807
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7089886A Pending JPS62228406A (en) | 1986-03-31 | 1986-03-31 | Operating method for melt reduction furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62228406A (en) |
-
1986
- 1986-03-31 JP JP7089886A patent/JPS62228406A/en active Pending
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