JPH01252714A - Mixed agglomerating briquette for smelting reduction furnace and smelting reduction method for mixed agglomerating briquette - Google Patents
Mixed agglomerating briquette for smelting reduction furnace and smelting reduction method for mixed agglomerating briquetteInfo
- Publication number
- JPH01252714A JPH01252714A JP7847988A JP7847988A JPH01252714A JP H01252714 A JPH01252714 A JP H01252714A JP 7847988 A JP7847988 A JP 7847988A JP 7847988 A JP7847988 A JP 7847988A JP H01252714 A JPH01252714 A JP H01252714A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- ore
- furnace
- iron ore
- smelting 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
Links
- 238000003723 Smelting Methods 0.000 title claims abstract description 11
- 238000000034 method Methods 0.000 title claims description 6
- 239000004484 Briquette Substances 0.000 title abstract description 12
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000003245 coal Substances 0.000 claims abstract description 30
- 229910052742 iron Inorganic materials 0.000 claims abstract description 16
- 230000001603 reducing effect Effects 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims abstract 3
- 238000002844 melting Methods 0.000 claims description 10
- 230000008018 melting Effects 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 abstract description 6
- 239000002893 slag Substances 0.000 abstract description 5
- 235000019738 Limestone Nutrition 0.000 abstract description 4
- 239000006028 limestone Substances 0.000 abstract description 4
- 238000005187 foaming Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000000843 powder Substances 0.000 abstract description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract 1
- 235000011941 Tilia x europaea Nutrition 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000004571 lime Substances 0.000 abstract 1
- 239000002994 raw material Substances 0.000 abstract 1
- 238000006722 reduction reaction Methods 0.000 description 23
- 239000007789 gas Substances 0.000 description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 229910052760 oxygen Inorganic materials 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 9
- 238000000354 decomposition reaction Methods 0.000 description 6
- 238000007664 blowing Methods 0.000 description 5
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 4
- 239000003575 carbonaceous material Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 235000012255 calcium oxide Nutrition 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000002747 voluntary effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/14—Multi-stage processes processes carried out in different vessels or furnaces
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Iron (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は溶融還元炉用混合塊成化ブリケット及びその溶
融還元方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a mixed agglomerated briquette for use in a melting reduction furnace and a method for melting and reducing the same.
[従来の技術]
例えば特開昭61−64807号公報に予備還元鉱石及
びチャーと、石炭とを混合、塊成化して得られるブリケ
ットを溶融還元炉に装入する方法が示されている。[Prior Art] For example, JP-A-61-64807 discloses a method in which briquettes obtained by mixing and agglomerating pre-reduced ore and char with coal are charged into a melting reduction furnace.
第4図にそのフローを示す。Figure 4 shows the flow.
即ち図において、鉄鉱石及び石灰石は、鉱石予熱炉1に
おいて、石炭と空気との燃焼反応熱によって加熱され、
流動層反応炉2に供給される。That is, in the figure, iron ore and limestone are heated in an ore preheating furnace 1 by the heat of combustion reaction between coal and air.
It is supplied to the fluidized bed reactor 2.
流動層反応炉2において、流動状態の予熱鉱石及び生石
灰に、石炭および酸素或は酸素含有ガスが吹込まれる。In the fluidized bed reactor 2, coal and oxygen or oxygen-containing gas are blown into the preheated ore and quicklime in a fluidized state.
吹込まれた石炭は、予熱鉱石との熱交換、及び酸素との
反応による部分燃焼により熱分解し、還元性のガスを発
生するとともに、チャーとなる。The injected coal is thermally decomposed through heat exchange with the preheated ore and partial combustion due to reaction with oxygen, generating reducing gas and turning into char.
溶融還元炉4では、上吹きランス5から酸素が浴に向っ
て吹きつけられるとともに、底吹羽口6から浴中に酸素
及び石炭等の炭材が吹込まれる。In the melting reduction furnace 4, oxygen is blown toward the bath from the top blowing lance 5, and oxygen and carbonaceous material such as coal are blown into the bath from the bottom blowing tuyere 6.
そして、供給されるブリケット17に含まれる炭材13
、底吹羽口6からの酸素とともに吹込まれる炭材、或は
装入装置7から供給されるコークスなどの炭材と、上吹
きランス5から供給される酸素との反応によって多量の
熱を発生する。Then, the carbon material 13 contained in the supplied briquettes 17
A large amount of heat is generated by the reaction between the carbonaceous material blown in together with oxygen from the bottom blowing tuyere 6 or the carbonaceous material such as coke supplied from the charging device 7 and the oxygen supplied from the top blowing lance 5. Occur.
この多量の熱によってブリケット17中の半還元鉱石は
溶解し、還元が進行し溶鉄19となる。The semi-reduced ore in the briquettes 17 is melted by this large amount of heat, and the reduction progresses to become molten iron 19.
この例では流動層反応炉2における予備還元工程生成物
を塊成化し、これを溶融還元炉4における溶鉄19とス
ラグ20界面或はその近傍で優先的に溶解・反応させる
。In this example, the product of the preliminary reduction process in the fluidized bed reactor 2 is agglomerated, and this is preferentially melted and reacted at or near the interface between the molten iron 19 and the slag 20 in the smelting reduction furnace 4.
[発明が解決しようとする課題]
混合塊成化物(ブリケット等)が鉄浴内に装入されると
外側より伝熱・溶解が起こるが、温度の上昇によりまず
石炭分解ガスが発生し、さらに高温になるとこのガスが
鉱石を還元する。混合塊成化物の中心部ほど伝熱に時間
を要するためガス発生と還元の開始に時間差が生じ、発
生ガスが仔効に還元に使われる割合が小さくなる。[Problem to be solved by the invention] When mixed agglomerates (briquettes, etc.) are charged into an iron bath, heat transfer and melting occurs from the outside, but due to the rise in temperature, coal decomposition gas is first generated, and then coal decomposition gas is generated. When heated, this gas reduces the ore. Since heat transfer takes longer in the center of the mixed agglomerate, there is a time lag between gas generation and the start of reduction, and the proportion of generated gas that is effectively used for reduction becomes smaller.
本発明は鉄浴式溶融還元炉において耐火物を保護し、定
常操業により生産性を向上せしめる塊成化ブリケット及
びその溶融還元性を提起するものである。The present invention proposes an agglomerated briquette that protects refractories in an iron bath type smelting reduction furnace and improves productivity through steady operation, and its smelting and reducing properties.
[課題を解決するための手段]
本発明は揮発分20%以上の石炭と還元率60%以上の
鉱石を、外層ほど鉱石比率が高くなるように鉱石と石炭
を混合して多層に形成した溶融還元炉用混合塊成化ブリ
ケットである。[Means for Solving the Problems] The present invention provides a molten coal with a volatile content of 20% or more and an ore with a reduction rate of 60% or more. This is a mixed agglomerated briquette for reduction furnaces.
更に本発明は流動層反応炉において鉄鉱石を予備還元し
て還元率60%以上の半還元鉱石を得て、別の系から供
給される揮発分20%以上の石炭とこの半還元鉱石を混
合して、外層ほど鉱石比率が高くなるように多層に形成
した塊成化ブリケットを鉄浴式溶融還元炉に装入し、前
記半還元鉱石を溶融還元することを特徴とする塊成化ブ
リケットの溶融還元方法である。Furthermore, the present invention pre-reduces iron ore in a fluidized bed reactor to obtain semi-reduced ore with a reduction rate of 60% or more, and mixes this semi-reduced ore with coal having a volatile content of 20% or more supplied from another system. The agglomerated briquettes formed in multiple layers such that the ore ratio becomes higher in the outer layer are charged into an iron bath type smelting reduction furnace, and the semi-reduced ore is melted and reduced. This is a melt reduction method.
本発明者らの実験によると混合塊成化物の中心部に石炭
を多く、外周部に鉱石を多く配することによって、石炭
分解ガスがより高温である外周部で鉱石の還元に効率よ
く使われる。According to experiments conducted by the present inventors, by arranging more coal in the center of the mixed agglomerate and more ore in the outer periphery, coal decomposition gas can be efficiently used to reduce ore in the outer periphery where the temperature is higher. .
即ち本発明のブリケットは第1図に示すように、揮発分
20%以上を有する石炭粉を内層核1とし、還元率60
%以下の部分還元鉱との混合物を外層2として多層に形
成される(第1図a)。That is, as shown in Fig. 1, the briquette of the present invention uses coal powder having a volatile content of 20% or more as the inner layer core 1, and has a reduction rate of 60%.
% or less of partially reduced ore as the outer layer 2 (Fig. 1a).
この例を第1表に示す。An example of this is shown in Table 1.
第 1 表
又層1を例えば揮発分2096以上の石炭リッチの半還
元鉱との混合層とするときは層3の外層は部分還元鉱リ
ッチとする。この例を第2表に示す。Table 1 In addition, when layer 1 is a mixed layer with semi-reduced ore rich in coal having a volatile content of 2096 or more, the outer layer of layer 3 is rich in partially reduced ore. An example of this is shown in Table 2.
第 2 表
従って本発明における内層及び外層は鉱石及び石炭が予
め定める比率で混合されることも含む。Table 2 Therefore, the inner layer and outer layer in the present invention also include ore and coal mixed in a predetermined ratio.
本発明のブリケットは鉄浴内に装入されるとき温度の上
昇により、石炭分解ガスを発生し、このガスが鉱石を還
元することとなるので揮発分が高い程好ましいが、少く
とも20%とする。When the briquettes of the present invention are charged into an iron bath, a rise in temperature generates coal decomposition gas, and this gas reduces the ore. do.
又ブリケットの外層となる予備還元鉱は、実験によると
少くとも60%の還元率をもつことが好ましい。According to experiments, the pre-reduced ore forming the outer layer of the briquettes preferably has a reduction rate of at least 60%.
次に本発明の塊成化ブリケットの溶解還元法について説
明する。第3図はそのフローを示す。Next, the method for melting and reducing agglomerated briquettes of the present invention will be explained. FIG. 3 shows the flow.
鉄鉱石及び石灰石は鉱石予熱炉1において加熱され流動
層反応炉2に供給される。流動層反応炉2は流動状態の
予熱鉱石に生石灰、石炭、酸素含有ガスが吹込まれ、吹
込まれた石炭は予熱鉱石との熱交換、熱分解し、チャー
化する。又還元ガス23は流動層反応炉に吹込まれ、石
炭の熱分解による還元性ガスとともに鉱石を半還元(6
0%以上)する。Iron ore and limestone are heated in an ore preheating furnace 1 and supplied to a fluidized bed reactor 2. In the fluidized bed reactor 2, quicklime, coal, and oxygen-containing gas are blown into the preheated ore in a fluidized state, and the blown coal exchanges heat with the preheated ore, thermally decomposes, and turns into char. In addition, the reducing gas 23 is blown into the fluidized bed reactor, and the ore is semi-reduced (6
0% or more).
予備還元された鉱石は石炭7とともに塊成化されて、中
心層に石炭7を多く、予備還元鉱を外層に多くもつブリ
ケットに形成する。このブリケットは装入装置8により
上吹転炉型溶解還元炉4に装入される。The pre-reduced ore is agglomerated together with coal 7 to form briquettes having more coal 7 in the center layer and more pre-reduced ore in the outer layer. The briquettes are charged into the top-blowing converter type melting and reduction furnace 4 by the charging device 8 .
炉内に装入されたブリケットは外周部から伝熱により昇
温し、500〜1000℃以上になると石炭分解ガスを
発生し、1000℃〜以上になると還元反応(I)、石
炭ガス化反応(n)が起こり、〜1500℃の高温にな
る程より活発に反応が起こる。The temperature of the briquettes charged into the furnace increases due to heat transfer from the outer periphery, and when the temperature reaches 500 to 1000°C or higher, coal decomposition gas is generated, and when the temperature reaches 1000°C or higher, reduction reaction (I) and coal gasification reaction ( n) occurs, and the reaction occurs more actively as the temperature increases to ~1500°C.
ブリケット中心部では昇温に時間がかかるため還元の開
始が遅れるが、発生ガスがより高温の外周部を通る時に
還元反応が進行し、還元が効率よく行われる。In the center of the briquette, the start of reduction is delayed because it takes time to raise the temperature, but when the generated gas passes through the outer periphery where the temperature is higher, the reduction reaction progresses and the reduction is carried out efficiently.
第2図は第1図(b)のブリケットを溶解還元したとき
の温度図表である。FIG. 2 is a temperature chart when the briquettes shown in FIG. 1(b) are melted and reduced.
即ち本発明のブリケットによると、ブリケットがスラグ
へ溶解する前にブリケット内での還元がよく進むので、
スラグ中酸化鉄濃度が低下する。That is, according to the briquette of the present invention, reduction within the briquette progresses well before the briquette dissolves into slag.
Iron oxide concentration in slag decreases.
[発明の効果]
本発明は石炭を内層にして半還元鉱を外層にもつブリケ
ットを用いるので、石炭分解ガスが発生し、高温になる
程鉱石還元反応が起るので、スラグフォーミングを抑え
、耐火物のFeOによる損傷を低減させることができる
。或はフォーミングによる操業限界の(T、Fe)近く
で定常操業して生産性を上げることができる。[Effect of the invention] Since the present invention uses a briquette with coal as the inner layer and semi-reduced ore as the outer layer, coal decomposition gas is generated, and as the temperature increases, the ore reduction reaction occurs, suppressing slag foaming and improving fire resistance. Damage to objects caused by FeO can be reduced. Alternatively, productivity can be increased by performing steady operation near the operational limit (T, Fe) due to forming.
第1図a、 bは本発明例の模式図、第2図は温度−
還元の図表、第3図は本発明の説明図、第4図は比較例
の説明図である。
2・・・流動層反応炉 4・・・溶解還元炉5・
・・酸素ランス
代 理 人 弁理士 茶野木 立 夫手続補正書(
自発)
昭和63年5月17日Figures 1a and b are schematic diagrams of the example of the present invention, and Figure 2 is a diagram showing the temperature -
FIG. 3 is an explanatory diagram of the present invention, and FIG. 4 is an explanatory diagram of a comparative example. 2... Fluidized bed reactor 4... Melting reduction furnace 5.
... Oxygen lance agent Patent attorney Tatsuo Chanoki Procedural amendment (
(Voluntary) May 17, 1986
Claims (1)
を、外層ほど鉱石比率が高くなるように鉱石と石炭を混
合して多層に形成した溶融還元炉用混合塊成化ブリケッ
ト。 2、流動層反応炉において鉄鉱石を予備還元して還元率
60%以上の半還元鉱石を得て、別の系から供給される
揮発分20%以上の石炭とこの半還元鉱石を混合して、
外層ほど鉱石比率が高くなるように多層に形成した塊成
化ブリケットを鉄浴式溶融還元炉に装入し、前記半還元
鉱石を溶融還元することを特徴とする塊成化ブリケット
の溶融還元方法。[Scope of Claims] 1. A mixture for a smelting reduction furnace in which coal with a volatile content of 20% or more and ore with a reduction rate of 60% or more are mixed and formed into multiple layers such that the ore ratio increases in the outer layer. Agglomerated briquettes. 2. Preliminarily reduce iron ore in a fluidized bed reactor to obtain semi-reduced ore with a reduction rate of 60% or more, and mix this semi-reduced ore with coal with a volatile content of 20% or more supplied from another system. ,
A method for melting and reducing agglomerated briquettes, characterized in that agglomerated briquettes formed in multiple layers such that the ore ratio becomes higher in the outer layer are charged into an iron bath type melting and reducing furnace, and the semi-reduced ore is melted and reduced. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7847988A JPH01252714A (en) | 1988-03-31 | 1988-03-31 | Mixed agglomerating briquette for smelting reduction furnace and smelting reduction method for mixed agglomerating briquette |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7847988A JPH01252714A (en) | 1988-03-31 | 1988-03-31 | Mixed agglomerating briquette for smelting reduction furnace and smelting reduction method for mixed agglomerating briquette |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01252714A true JPH01252714A (en) | 1989-10-09 |
Family
ID=13663138
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7847988A Pending JPH01252714A (en) | 1988-03-31 | 1988-03-31 | Mixed agglomerating briquette for smelting reduction furnace and smelting reduction method for mixed agglomerating briquette |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01252714A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2728590A1 (en) * | 1994-12-26 | 1996-06-28 | Po Hang Iron & Steel | METHOD FOR THE AGGLOMERATION OF HOT IRON ORE PARTICLES PRE-REDUCED FOR THE PRODUCTION OF IRON IN SLABS |
EP0743368A1 (en) * | 1995-05-18 | 1996-11-20 | Technological Resources Pty. Ltd. | A smelting reduction method with increased effectiveness |
WO2006004350A1 (en) * | 2004-06-30 | 2006-01-12 | Posco | Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same |
WO2006006820A1 (en) * | 2004-07-12 | 2006-01-19 | Posco | Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same |
WO2006009371A1 (en) * | 2004-07-16 | 2006-01-26 | Posco | Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same. |
WO2014031801A1 (en) * | 2012-08-22 | 2014-02-27 | Hoffman Glenn E | Production of pig iron |
WO2014031802A1 (en) * | 2012-08-22 | 2014-02-27 | Hoffman Glenn E | Producing pig iron from iron-containing feed materials |
-
1988
- 1988-03-31 JP JP7847988A patent/JPH01252714A/en active Pending
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2728590A1 (en) * | 1994-12-26 | 1996-06-28 | Po Hang Iron & Steel | METHOD FOR THE AGGLOMERATION OF HOT IRON ORE PARTICLES PRE-REDUCED FOR THE PRODUCTION OF IRON IN SLABS |
EP0743368A1 (en) * | 1995-05-18 | 1996-11-20 | Technological Resources Pty. Ltd. | A smelting reduction method with increased effectiveness |
AU678746B2 (en) * | 1995-05-18 | 1997-06-05 | Technological Resources Pty Limited | A smelting reduction method with increased effectiveness |
AU678746C (en) * | 1995-05-18 | 2002-01-03 | Technological Resources Pty Limited | A smelting reduction method with increased effectiveness |
WO2006004350A1 (en) * | 2004-06-30 | 2006-01-12 | Posco | Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same |
WO2006006820A1 (en) * | 2004-07-12 | 2006-01-19 | Posco | Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same |
US7588717B2 (en) | 2004-07-12 | 2009-09-15 | Posco | Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same |
WO2006009371A1 (en) * | 2004-07-16 | 2006-01-26 | Posco | Apparatus for manufacturing compacted irons of reduced materials comprising fine direct reduced irons and apparatus for manufacturing molten irons using the same. |
WO2014031801A1 (en) * | 2012-08-22 | 2014-02-27 | Hoffman Glenn E | Production of pig iron |
WO2014031802A1 (en) * | 2012-08-22 | 2014-02-27 | Hoffman Glenn E | Producing pig iron from iron-containing feed materials |
AU2013305777B2 (en) * | 2012-08-22 | 2015-07-16 | Hoffman And Sons Technologies, Llc | Producing pig iron from iron-containing feed materials |
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