JPH0561323B2 - - Google Patents
Info
- Publication number
- JPH0561323B2 JPH0561323B2 JP15666389A JP15666389A JPH0561323B2 JP H0561323 B2 JPH0561323 B2 JP H0561323B2 JP 15666389 A JP15666389 A JP 15666389A JP 15666389 A JP15666389 A JP 15666389A JP H0561323 B2 JPH0561323 B2 JP H0561323B2
- Authority
- JP
- Japan
- Prior art keywords
- ore
- reduction furnace
- fallen
- amount
- riser
- 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 - Lifetime
Links
- 238000003723 Smelting Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims 1
- 239000000843 powder Substances 0.000 description 7
- 239000002994 raw material Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、鉄鉱石粉及び石炭を使用して銑鉄を
製造する溶融還元技術に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a smelting reduction technique for producing pig iron using iron ore powder and coal.
近時、特開昭58−217615号公報に見られるよう
に循環流動層型予備還元炉の実験を実施した結
果、約15〜30t/d規模の予備還元炉で約100〜
300Kg/hの落鉱があり、鉱石の種類や操業条件
によつてはかなりの落鉱量が予想される。一般
に、鉱石は粉鉱石を使用するが、中には粒径の粗
いものもあることや操業上鉱石のステイツキング
を起し、落鉱を完全に防止することは非常に困難
と考えられる。
Recently, as seen in Japanese Patent Application Laid-Open No. 58-217615, we conducted an experiment on a circulating fluidized bed pre-reduction reactor, and found that a pre-reduction reactor with a scale of about 15-30 t/d can reduce
The amount of ore falling is 300Kg/h, and depending on the type of ore and operating conditions, a considerable amount of ore is expected to fall. Generally, powdered ore is used, but it is considered extremely difficult to completely prevent ore from falling due to the fact that some of the ore has a coarse particle size and statesking of ore occurs during operation.
第2図は従来の装置の縦断面図で、ライザー1
内で下から吹上げる還元ガス20によつて流動予
備還元された粉鉱石はサイクロン2において還元
ガスと分離され、ダウンカマ3を通つて粉鉱石循
環装置4を経てライザー1に戻される。原料粉鉱
石11はライザー出口気流中に供給され、予備還
元された鉱石はダウンカマ3から抜出される。 Figure 2 is a vertical cross-sectional view of the conventional device, with riser 1
The fine ore which has been preliminarily reduced by the reducing gas 20 blown up from below is separated from the reducing gas in the cyclone 2 and is returned to the riser 1 via the downcomer 3 and the fine ore circulation device 4. The raw material powder ore 11 is supplied into the riser outlet air stream, and the pre-reduced ore is extracted from the downcomer 3.
一般的に、第2図に示すような循環流動層型予
備還元炉では還元ガス20の上昇流に逆らつて落
下するライザー1の下部からの落鉱を完全に防止
することは困難である。
Generally, in a circulating fluidized bed pre-reduction furnace as shown in FIG. 2, it is difficult to completely prevent ore from falling from the lower part of the riser 1, which falls against the upward flow of the reducing gas 20.
本発明は効果的な落鉱処理の方法を提供する。 The present invention provides an effective method for treating fallen mines.
第1図に従つて、本発明の手段を説明する。5
は二段羽口を有する溶融還元炉であり、該還元炉
5より発生する還元ガス20は排ガスダクト8を
介して循環流動層型予備還元炉のライザー1内に
供給される。一方、原料粉鉱石11はライザー1
の出口部に供給され、サイクロン2で捕集され、
ダウンカマ3に滞留し、循環装置4で再びライザ
ー1に戻され循環する。
The means of the present invention will be explained with reference to FIG. 5
is a smelting reduction furnace having two-stage tuyeres, and reducing gas 20 generated from the reduction furnace 5 is supplied through an exhaust gas duct 8 into the riser 1 of the circulating fluidized bed pre-reduction furnace. On the other hand, the raw material powder ore 11 is
is supplied to the outlet of the cyclone 2, collected by cyclone 2,
It stays in the downcomer 3, is returned to the riser 1 again by the circulation device 4, and is circulated.
通常還元された鉱石はダウンカマ3より排出さ
れホツパ7に貯蔵され、還元炉5の上段羽口へ投
入される。 Normally, the reduced ore is discharged from the downcomer 3, stored in the hopper 7, and introduced into the upper tuyere of the reduction furnace 5.
本発明はライザー1の下方にホツパ6を設け、
落鉱した鉱石を還元炉5の炉頂へ投入するように
したものである。 The present invention provides a hopper 6 below the riser 1,
The fallen ore is charged into the top of the reduction furnace 5.
本発明によれば循環流動層型予備還元炉のライ
ザー1より落鉱した鉱石が一旦、ホツパ6に貯蔵
され、該ホツパ6から溶融還元炉5の炉頂に上記
落鉱を投入できる装入管を設けることにより落鉱
が直接溶融還元できるようになる。
According to the present invention, the ore that has fallen from the riser 1 of the circulating fluidized bed pre-reduction furnace is temporarily stored in the hopper 6, and the charging pipe through which the ore can be charged from the hopper 6 to the top of the smelting reduction furnace 5. By providing this, the fallen ore can be directly melted and reduced.
第1図は本発明方法の実施例の全体フロー図で
ある。第1図において、予備還元炉への原料粉鉱
石11の供給量が600Kg/h、溶融還元炉からの
ガス発生量20が3000Nm3/h、ライザー内の粉鉱
石滞留量が800Kg、原料粉鉱石の粒径が平均
50μm、原料粉鉱石の見掛け比重が4.2の実操業結
果では、溶融還元炉の上段羽口より投入される予
備還元鉱15の量が400〜450Kg/h、溶融還元炉
5の炉頂より装入される粉鉱石量が100〜150Kg/
hであつた。
FIG. 1 is an overall flow diagram of an embodiment of the method of the present invention. In Figure 1, the amount of raw ore powder 11 supplied to the preliminary reduction furnace is 600 kg/h, the amount of gas generated 20 from the smelting reduction furnace is 3000 Nm 3 /h, the amount of fine ore retained in the riser is 800 kg, and the amount of raw ore powder 11 is 600 kg/h. The average particle size of
50μm, and the apparent specific gravity of raw material powder ore is 4.2, the amount of pre-reduced ore 15 charged from the upper tuyere of the smelting reduction furnace is 400 to 450 kg/h, and the amount of pre-reduced ore 15 is charged from the top of the smelting reduction furnace 5. The amount of fine ore produced is 100 to 150 kg/
It was h.
この結果からもわかるように、上記循環流動層
型予備還元炉の操業では、落鉱量が原料粉鉱石供
給量の15〜25%もあり、これを溶融還元炉に装入
せず、系外へ排出し再び事前処理して予備還元炉
に投入するとか、溶融還元炉に装入するというの
は、処理量からして相当な付帯設備が必要とな
る。本発明方法では、上記のような複雑な付帯設
備も必要なく簡単に落鉱が処理可能となつた。 As can be seen from this result, in the operation of the above-mentioned circulating fluidized bed pre-reduction furnace, the amount of fallen ore is 15 to 25% of the amount of raw powder ore supplied, and this is not charged to the smelting reduction furnace and is removed outside the system. Considering the throughput, a considerable amount of ancillary equipment is required to discharge the waste into a tank, pre-process it again, and then charge it into a preliminary reduction furnace, or to charge it into a smelting reduction furnace. With the method of the present invention, fallen ore can be easily treated without the need for complicated incidental equipment as described above.
本発明によれば予備還元炉の落鉱を直接溶融還
元炉に投入することにより熱効率および歩留りが
向上する。
According to the present invention, the thermal efficiency and yield are improved by directly charging the fallen ore from the preliminary reduction furnace to the smelting reduction furnace.
第1図は本発明の実施例の全体フロー図、第2
図は循環流動層型予備還元炉の縦断面図である。
1……ライザー、2……サイクロン、3……ダ
ウンカマ、4……鉱石循環装置、5……溶融還元
炉、6……落鉱ホツパ、7……予備還元鉱ホツ
パ、8……排ガスダクト。
Fig. 1 is an overall flow diagram of an embodiment of the present invention;
The figure is a longitudinal sectional view of a circulating fluidized bed pre-reduction furnace. 1... riser, 2... cyclone, 3... downcomer, 4... ore circulation device, 5... smelting reduction furnace, 6... falling ore hopper, 7... preliminary reduced ore hopper, 8... exhaust gas duct.
Claims (1)
の操業において、該予備還元炉で発生する落鉱鉱
石をホツパに一時的に貯蔵し、該落鉱鉱石を上記
溶融還元炉内の炭材流動層内に装入することを特
徴とする予備還元炉の落鉱処理方法。1. In the operation of a smelting reduction furnace having a circulating fluidized bed type pre-reduction furnace, the fallen ore generated in the pre-reduction furnace is temporarily stored in a hopper, and the fallen ore is transferred to the carbonaceous fluid in the smelting reduction furnace. A method for treating fallen ore in a preliminary reduction furnace, characterized by charging the ore within a layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15666389A JPH0324213A (en) | 1989-06-21 | 1989-06-21 | Treatment of drop ore of preliminary reduction furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15666389A JPH0324213A (en) | 1989-06-21 | 1989-06-21 | Treatment of drop ore of preliminary reduction furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0324213A JPH0324213A (en) | 1991-02-01 |
JPH0561323B2 true JPH0561323B2 (en) | 1993-09-06 |
Family
ID=15632584
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15666389A Granted JPH0324213A (en) | 1989-06-21 | 1989-06-21 | Treatment of drop ore of preliminary reduction furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0324213A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2300008B (en) * | 1995-04-19 | 1999-04-14 | Nippon Cable System Inc | Seat-lifting device for a stool |
-
1989
- 1989-06-21 JP JP15666389A patent/JPH0324213A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH0324213A (en) | 1991-02-01 |
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