JP2014132122A5 - - Google Patents
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- JP2014132122A5 JP2014132122A5 JP2014068059A JP2014068059A JP2014132122A5 JP 2014132122 A5 JP2014132122 A5 JP 2014132122A5 JP 2014068059 A JP2014068059 A JP 2014068059A JP 2014068059 A JP2014068059 A JP 2014068059A JP 2014132122 A5 JP2014132122 A5 JP 2014132122A5
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- blast furnace
- operating method
- ton
- partially reduced
- reduced iron
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(実施例1、参考例1)
図1に示すような高炉(内容積:1600m3)に、酸化鉄原料及びコークスを装入するとともに、羽口から酸素富化空気及び微粉炭を吹き込んで、溶銑の製造を行った。そして、部分還元鉄(金属化率:82%、炭素含有率:3.5%)を100kg/ton装入し、図3に示す操作を行って、高炉の安定操業が可能な運転条件を求めた。その結果を図4にプロットした。実施例1及び参考例1では、図4にプロットされたいくつかの運転条件のうち、酸素富化率:13.2%、微粉炭比:238kg/tonの運転条件で、出銑比を2.87ton/d/m3にすることができた。
(Example 1 , Reference Example 1 )
A blast furnace (inner volume: 1600 m 3 ) as shown in FIG. 1 was charged with iron oxide raw material and coke, and oxygen-enriched air and pulverized coal were blown from the tuyere to produce hot metal. Then, partially reduced iron (metalization rate: 82%, carbon content: 3.5%) is charged at 100 kg / ton, and the operation shown in FIG. It was. The results are plotted in FIG. In Example 1 and Reference Example 1 , among several operating conditions plotted in FIG. 4, the output ratio was 2 under the operating conditions of oxygen enrichment rate: 13.2% and pulverized coal ratio: 238 kg / ton. .87 ton / d / m 3 .
(実施例2、参考例2)
部分還元鉄の装入量を200kg/tonとしたこと以外は、実施例1及び参考例1と同様にして、高炉の安定操業が可能な運転条件を求めた。その結果を図4にプロットした。実施例2及び参考例2では、図4にプロットされたいくつかの運転条件のうち、酸素富化率:16%、微粉炭比:237kg/tonの運転条件で、出銑比を2.94ton/d/m3にすることができた。
(Example 2 and Reference Example 2 )
The operating conditions under which stable operation of the blast furnace was possible were determined in the same manner as in Example 1 and Reference Example 1 except that the amount of partially reduced iron charged was 200 kg / ton. The results are plotted in FIG. In Example 2 and Reference Example 2 , among several operating conditions plotted in FIG. 4, the oxygen enrichment ratio: 16%, the pulverized coal ratio: 237 kg / ton, and the output ratio is 2.94 ton. / D / m 3 .
(実施例3、参考例3)
部分還元鉄の装入量を300kg/tonとしたこと以外は、実施例1及び参考例1と同様にして、高炉の安定操業が可能な運転条件を求めた。その結果を図4にプロットした。実施例3及び参考例3では、図4にプロットされたいくつかの運転条件のうち、酸素富化率:16%、微粉炭比:225kg/tonの運転条件で、出銑比を3.09ton/d/m3にすることができた。
(Example 3 , Reference Example 3 )
The operating conditions under which stable operation of the blast furnace was possible were determined in the same manner as in Example 1 and Reference Example 1 except that the amount of partially reduced iron charged was 300 kg / ton. The results are plotted in FIG. In Example 3 and Reference Example 3 , among several operating conditions plotted in FIG. 4, the oxygen enrichment ratio: 16%, the pulverized coal ratio: 225 kg / ton, and the output ratio is 3.09 ton. / D / m 3 .
(実施例4、参考例4)
部分還元鉄の装入量を400kg/tonとしたこと以外は、実施例1及び参考例1と同様にして、高炉の安定操業が可能な運転条件を求めた。その結果を図4にプロットした。実施例4及び参考例4では、図4にプロットされたいくつかの運転条件のうち、酸素富化率:14%、微粉炭比:210kg/tonの運転条件で、出銑比を3.25ton/d/m3にすることができた。
(Example 4 , Reference Example 4 )
The operating conditions under which stable operation of the blast furnace was possible were determined in the same manner as in Example 1 and Reference Example 1 except that the amount of partially reduced iron charged was 400 kg / ton. The results are plotted in FIG. In Example 4 and Reference Example 4 , among several operating conditions plotted in FIG. 4, the oxygen enrichment ratio: 14%, the pulverized coal ratio: 210 kg / ton, and the output ratio is 3.25 ton. / D / m 3 .
(実施例5、参考例5)
部分還元鉄の装入量を500kg/tonとしたこと以外は、実施例1及び参考例1と同様にして、高炉の安定操業が可能な運転条件を求めた。その結果を図4にプロットした。実施例5及び参考例5では、図4にプロットされたいくつかの運転条件のうち、酸素富化率:14%、微粉炭比:198kg/tonの運転条件で、出銑比を3.44ton/d/m3にすることができた。
(Example 5 , Reference Example 5 )
The operating conditions under which stable operation of the blast furnace was possible were determined in the same manner as in Example 1 and Reference Example 1 except that the amount of partially reduced iron charged was 500 kg / ton. The results are plotted in FIG. In Example 5 and Reference Example 5 , among several operating conditions plotted in FIG. 4, the oxygen enrichment ratio: 14%, the pulverized coal ratio: 198 kg / ton, and the output ratio is 3.44 ton. / D / m 3 .
(実施例6、参考例6)
部分還元鉄の装入量を600kg/tonとしたこと以外は、実施例1及び参考例1と同様にして、高炉の安定操業が可能な運転条件を求めた。その結果を図4にプロットした。実施例6及び参考例6では、図4にプロットされたいくつかの運転条件のうち、酸素富化率:14%、微粉炭比:190kg/tonの運転条件で、出銑比を3.63ton/d/m3にすることができた。
(Example 6 , Reference Example 6 )
The operating conditions under which stable operation of the blast furnace was possible were determined in the same manner as in Example 1 and Reference Example 1 except that the amount of partially reduced iron charged was 600 kg / ton. The results are plotted in FIG. In Example 6 and Reference Example 6 , among several operating conditions plotted in FIG. 4, the oxygen enrichment ratio: 14%, the pulverized coal ratio: 190 kg / ton, and the output ratio is 3.63 ton. / D / m 3 .
Claims (8)
前記酸素富化空気の酸素富化率をx(%)、及び、溶銑1ton当たりの前記微粉炭の吹き込み量をy(kg/ton)としたときに、x及びyが、下記式(1)〜(3)を満たす高炉の操業方法。
25x−175<y<31x+31 (1)
y>130 (2)
x>8 (3) A blast furnace in which iron oxide raw material, coke and partially reduced iron are charged from the top of the blast furnace, and pulverized coal and oxygen-enriched air are blown from the tuyere of the blast furnace to reduce the iron oxide raw material to obtain molten iron Operating method,
When the oxygen enrichment rate of the oxygen-enriched air is x (%) and the amount of the pulverized coal per 1 ton of hot metal is y (kg / ton), x and y are expressed by the following formula (1) Blast furnace operation method satisfying (3) .
25x-175 <y <31x + 31 ( 1 )
y> 130 ( 2 )
x> 8 (3)
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JP2014068059A JP5693768B2 (en) | 2012-12-07 | 2014-03-28 | Blast furnace operating method and hot metal manufacturing method |
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JP2014068059A JP5693768B2 (en) | 2012-12-07 | 2014-03-28 | Blast furnace operating method and hot metal manufacturing method |
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JP2013214049A Division JP5546675B1 (en) | 2012-12-07 | 2013-10-11 | Blast furnace operating method and hot metal manufacturing method |
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JP2014132122A JP2014132122A (en) | 2014-07-17 |
JP2014132122A5 true JP2014132122A5 (en) | 2014-10-09 |
JP5693768B2 JP5693768B2 (en) | 2015-04-01 |
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Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH0913109A (en) * | 1995-06-29 | 1997-01-14 | Kawasaki Steel Corp | Operation of blowing large quantity of pulverized fine coal into blast furnace |
JP3589016B2 (en) * | 1998-04-03 | 2004-11-17 | 住友金属工業株式会社 | Blast furnace operation method |
JP2001073016A (en) * | 1999-09-08 | 2001-03-21 | Sumitomo Metal Ind Ltd | Operation of blast furnace |
JP2001131616A (en) * | 1999-11-11 | 2001-05-15 | Nkk Corp | Method of operating blast and method of operating sintering furnace |
JP2001234213A (en) * | 2000-02-28 | 2001-08-28 | Nippon Steel Corp | Blast furnace operation method |
JP2003247008A (en) * | 2002-02-25 | 2003-09-05 | Jfe Steel Kk | Method for operating blast furnace injecting a large amount of pulverized fine coal |
JP4061135B2 (en) * | 2002-06-24 | 2008-03-12 | 新日本製鐵株式会社 | Blast furnace operation method with pulverized coal injection |
JP4910640B2 (en) * | 2006-10-31 | 2012-04-04 | Jfeスチール株式会社 | Blast furnace operation method |
JP5059379B2 (en) * | 2006-11-16 | 2012-10-24 | 株式会社神戸製鋼所 | Hot briquette iron for blast furnace charging raw material and method for producing the same |
UA96505C2 (en) * | 2007-09-14 | 2011-11-10 | Ниппон Стил Корпорейшен | Method for producing of reduced iron pellets and method for production of open-hearth pig iron |
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