JPH07166250A - Production of sintered ore using metallic iron - Google Patents
Production of sintered ore using metallic ironInfo
- Publication number
- JPH07166250A JPH07166250A JP5344629A JP34462993A JPH07166250A JP H07166250 A JPH07166250 A JP H07166250A JP 5344629 A JP5344629 A JP 5344629A JP 34462993 A JP34462993 A JP 34462993A JP H07166250 A JPH07166250 A JP H07166250A
- Authority
- JP
- Japan
- Prior art keywords
- sintering
- hot air
- metallic iron
- raw material
- ore
- 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
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
- Y02P10/10—Reduction of greenhouse gas [GHG] emissions
- Y02P10/122—Reduction of greenhouse gas [GHG] emissions by capturing or storing CO2
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は焼結鉱製造分野におい
て、熱風循環システムを加えることにより、メタリック
鉄の酸化発熱反応を促進することを利用した製造方法で
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is a production method in the field of sinter ore production, which utilizes the addition of a hot air circulation system to promote the oxidation exothermic reaction of metallic iron.
【0002】[0002]
【従来の技術】従来、焼結鉱製造熱源として粉コークス
を使用し、この燃焼熱により、溶融結合させて焼結を行
っていた。2. Description of the Related Art Conventionally, powder coke has been used as a heat source for the production of sinter, and the combustion heat has been used to cause fusion and sintering.
【0003】[0003]
【発明が解決しようとする課題】メタリック鉄を熱源と
する焼結反応に、焼結機より発生する熱風又は熱交換さ
れた清浄熱風を利用する事により燃料費低減と同時に排
ガスの低NOx、低CO2化を図ることを本発明の課題
とした。By using hot air generated from a sintering machine or clean hot air that has been heat-exchanged in the sintering reaction using metallic iron as a heat source, fuel cost can be reduced and at the same time low NOx and low exhaust gas can be obtained. The object of the present invention was to achieve CO 2 conversion.
【0004】[0004]
【課題を解決するための手段】このため、本発明は、メ
タリック鉄を熱源として、さらに高温熱風及び清浄熱風
を焼結ベッドに吹き込んでメタリック鉄の酸化発熱反応
を促進させることにより焼結に必要な熱量を供給する。Therefore, the present invention is required for sintering by using metallic iron as a heat source and further blowing hot hot air and clean hot air into the sintering bed to promote the oxidation exothermic reaction of the metallic iron. Supply a certain amount of heat.
【0005】[0005]
【作用】上記のように、粉コークスの燃焼熱による従来
の焼結方法を、本発明による熱風循環システムを付加
し、メタリック鉄の酸化発熱反応を促進した焼結方法に
変える事により、燃料費低減、低NOx、低CO2の完
全焼結を行うことが出来る。As described above, by changing the conventional sintering method using the combustion heat of powder coke to a sintering method in which the hot air circulation system according to the present invention is added to promote the oxidation exothermic reaction of metallic iron, the fuel cost can be reduced. Reduction, low NOx, low CO 2 complete sintering can be performed.
【0006】[0006]
【実施例】表1に本焼結方法に使用される原料配合割合
を示す。 図1は、本発明の焼結鉱製造プロセスから発生する熱風
を、一部清浄熱風に熱交換させて焼結ベッドに送り込む
熱風循環システムフローの一例である。本例では、1、
シンタリングベッド末端より吸引された熱風が2、3、
集塵装置を経て4、熱交換器に入り、さらに5、No.
1フードよりシンタリングベッドに吹き込まれ、一方
6、ブロアーより送り込まれ熱交換された100℃以上
の清浄熱風は7、No.2フードよりシンタリングベッ
ドに吹き込むものである。EXAMPLES Table 1 shows the raw material compounding ratios used in the present sintering method. FIG. 1 is an example of a hot air circulation system flow in which hot air generated from the sintered ore manufacturing process of the present invention is partially heat-exchanged with clean hot air and sent to the sintering bed. In this example, 1,
The hot air sucked from the end of the sintering bed is 2, 3,
After entering the heat exchanger through the dust collector 4, the No. 5
No. 6, clean hot air blown from the hood 1 into the sintering bed, while being sent from the blower 6 and exchanged heat, was No. 7 It blows into the sintering bed from 2 hoods.
【0007】図2は、メタリック鉄を25mass
(%)含む焼結方法による焼結鉱化学分析値の一例を示
す。成分値によれば、粉コークス焼結方法によるもの
と、大きな変化はない。[0007] FIG. 2 shows 25 mass of metallic iron.
An example of the sinter ore chemical analysis value by the sintering method including (%) is shown. According to the component values, there is no significant change from the powder coke sintering method.
【0008】図3は、従来の粉コークス焼結方法とメタ
リック鉄を25mass(%)含む焼結方法のNOx排
出量、還元粉化率、常温強度を比較した一例で、NOx
排出量は従来型焼結に対し、55.9% 低減されてい
る。還元粉化率は若干悪化しているが、変化量が小さ
く、又常温強度はほぼ同一であり、高炉の要求する品質
を十分に満たしている。FIG. 3 shows an example of comparison of NOx emission amount, reduction pulverization rate, and room temperature strength between the conventional powder coke sintering method and the sintering method containing 25 mass% of metallic iron.
Emissions are reduced by 55.9% compared to conventional sintering. Although the reduction powdering rate is slightly worse, the amount of change is small, and the room temperature strength is almost the same, and the quality required by the blast furnace is sufficiently satisfied.
【0009】図4は、従来型焼結時及び本発明焼結時の
メタリック鉄を25mass(%)含む焼結方法の原料
層の中層部に於ける温度変化の一例を示す。高温熱風の
一部や清浄熱風を焼結ベッドへとリターンするシステム
により、図に示す如くメタリック鉄の酸化反応が効率的
に行われ、焼結開始点が従来型焼結に較べて早くなっ
た。FIG. 4 shows an example of temperature change in the middle layer of the raw material layer in the sintering method containing 25 mass% of metallic iron during the conventional sintering and the sintering according to the present invention. As shown in the figure, the oxidation reaction of metallic iron is efficiently performed by the system that returns part of the high-temperature hot air or clean hot air to the sintering bed, and the starting point of sintering is faster than in conventional sintering. .
【0010】[0010]
【発明の効果】本発明にあっては、従来の粉コークスを
熱源とする焼結方法に比較して、熱風循環システムを付
加し、メタリック鉄の大量使用を可能とした焼結方法の
ため、下記のような効果を得ることが出来る。 1)従来の焼結熱源としての粉コークスの代替として、
全量メタリック鉄におきかえが可能である。 2)従って従来の焼結熱源としての粉コークスは燃焼時
にNOx、CO2が多量に発生するが、本発明による方
法は、メタリック鉄に窒素が含まれないためこれから入
るNOxは零であり、又メタリック鉄の酸化発熱反応を
利用するためCO2の発生も少なくする事ができる。 3)熱風循環システムにより、メタリック鉄の酸化発熱
反応を促進する熱のリサイクルが行われ、省エネルギー
が出来る。EFFECTS OF THE INVENTION In the present invention, as compared with the conventional sintering method using coke powder as a heat source, a hot air circulation system is added, and the sintering method enables large-scale use of metallic iron. The following effects can be obtained. 1) As an alternative to the powder coke as a conventional sintering heat source,
It is possible to replace the entire amount with metallic iron. 2) Therefore, a large amount of NOx and CO 2 are generated during combustion in the conventional powder coke as a sintering heat source, but in the method according to the present invention, since NO is not contained in the metallic iron, NOx that enters from this is zero, and Since the oxidation exothermic reaction of metallic iron is used, the generation of CO 2 can be reduced. 3) The hot air circulation system recycles the heat that promotes the oxidation exothermic reaction of metallic iron, thus saving energy.
【図1】 本発明の熱風循環システムのフロー概要図で
ある。FIG. 1 is a flow schematic diagram of a hot air circulation system of the present invention.
【図2】 メタリック鉄を25mass(%)含む焼結
鉱の成品化学分析値を示す表である。FIG. 2 is a table showing chemical product analysis values of a sintered ore containing 25 mass (%) of metallic iron.
【図3】 従来型焼結法及び本発明焼結法のNOx排出
量、還元粉化率、常温強度の比較表である。FIG. 3 is a comparison table of NOx emission amount, reduction pulverization rate, and room temperature strength of the conventional sintering method and the sintering method of the present invention.
【図4】 焼結原料層の中層部に於ける温度変化を示す
図である。FIG. 4 is a diagram showing a temperature change in a middle layer portion of a sintering raw material layer.
1.シンタリングベッド 2.1次プレダスター 3.2次プレダスター、マルチサイクロン 4.熱交換器 5.No.1循環フード 6.冷風ブロアー 7.No.2循環フード 1. Sintering bed 2. Primary preduster 3. Secondary preduster, multi cyclone 4. Heat exchanger 5. No. 1. Circulating hood 6. Cold air blower 7. No. 2 circulation hood
Claims (2)
セスにおいて、そのプロセスから発生する熱風、もしく
は熱交換器により熱交換された100℃以上の清浄熱風
を焼結ベッドに吹き込むことにより、メタリック鉄表面
の活性度が上がり、酸化反応が促進され、焼結速度が向
上する事を利用した焼結鉱製造方法。1. In a sinter production process in which metallic iron is blended, hot air generated from the process or clean hot air of 100 ° C. or higher heat-exchanged by a heat exchanger is blown into the sintering bed to produce metallic iron. A method for producing sinter that utilizes the fact that the surface activity increases, the oxidation reaction is promoted, and the sintering rate is improved.
循環に加え、従来のボイラーに代わる、高温熱風と清浄
空気の熱交換を行い、清浄熱風を得ることにより、熱風
風量を増加させる熱風循環システム。2. In addition to circulating high-temperature hot air from the wind box under the sintering bed, heat exchange between high-temperature hot air and clean air, which replaces the conventional boiler, is performed to obtain clean hot air, thereby increasing the amount of hot air. Hot air circulation system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5344629A JPH07166250A (en) | 1993-12-08 | 1993-12-08 | Production of sintered ore using metallic iron |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5344629A JPH07166250A (en) | 1993-12-08 | 1993-12-08 | Production of sintered ore using metallic iron |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07166250A true JPH07166250A (en) | 1995-06-27 |
Family
ID=18370745
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5344629A Pending JPH07166250A (en) | 1993-12-08 | 1993-12-08 | Production of sintered ore using metallic iron |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07166250A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113249566A (en) * | 2021-03-03 | 2021-08-13 | 广西北港新材料有限公司 | Sintering system and method for limonite type laterite-nickel ore |
CN115323165A (en) * | 2022-06-08 | 2022-11-11 | 中南大学 | Sintered carbon emission reduction method for coupling hydrogen-rich gas and solid waste containing metallic iron for heat supply |
-
1993
- 1993-12-08 JP JP5344629A patent/JPH07166250A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113249566A (en) * | 2021-03-03 | 2021-08-13 | 广西北港新材料有限公司 | Sintering system and method for limonite type laterite-nickel ore |
CN113249566B (en) * | 2021-03-03 | 2023-02-07 | 广西北港新材料有限公司 | Sintering system and method for limonite type laterite-nickel ore |
CN115323165A (en) * | 2022-06-08 | 2022-11-11 | 中南大学 | Sintered carbon emission reduction method for coupling hydrogen-rich gas and solid waste containing metallic iron for heat supply |
CN115323165B (en) * | 2022-06-08 | 2023-11-10 | 中南大学 | Sintered carbon emission reduction method for coupling heating of hydrogen-rich fuel gas and solid waste containing metallic iron |
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