JPH0430455B2 - - Google Patents
Info
- Publication number
- JPH0430455B2 JPH0430455B2 JP13462386A JP13462386A JPH0430455B2 JP H0430455 B2 JPH0430455 B2 JP H0430455B2 JP 13462386 A JP13462386 A JP 13462386A JP 13462386 A JP13462386 A JP 13462386A JP H0430455 B2 JPH0430455 B2 JP H0430455B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- gas
- ore
- amount
- heat
- 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
Links
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 10
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- 238000007664 blowing Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 229910000863 Ferronickel Inorganic materials 0.000 claims description 2
- 239000000571 coke Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000002253 acid Substances 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229910002555 FeNi Inorganic materials 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
(産業上の利用分野)
本発明は、高炉によるフエロニツケルの製造方
法に関する。
(従来技術及びその問題点)
ニツケル原料鉱石は、ニツケルが約2%と品位
が低く、付着水及び結晶水が約30%と多く、通常
乾燥、ペレタイジング等の予備処理が必要であ
る。従来は一般にニツケル鉱石をキルン又はシヤ
フト炉で還元し、電気炉で溶解して製造されてお
り、溶鉱炉を用いる方法は、一部しか行われてい
ない。しかし溶鉱炉を用いた場合、フエロニツケ
ルの原料中に水分が多いため、水分の蒸発に多く
の燃料を食い、コークス比の上昇、炉頂温度の上
昇、生産性の低下などの問題がある。
(発明が解決しようとする技術的課題)
本発明は、コークス比を下げ、炉頂ガス温度を
下げ、生産性を向上できるフエロニツケルの製造
方法を提供することを目的とする。
(技術的課題を解決する手段)
本発明は、フエロニツケル鉱石を炉上部から挿
入し、羽口から熱風を吹込むとともに炉中段のシ
ヤフト部から予熱ガスを吹込むことを特徴とする
フエロニツケルの製造方法である。
(実施例)
以下本発明の実施例を図面を参照して説明す
る。第1図に示すように、ニツケル鉱石を乾燥後
篩分けし、塊鉱石はそのまま高炉1の炉頂から挿
入し、粉鉱石は造粒してグリーンボールとして高
炉1に挿入し、あるいは造粒後コールドボンドと
して高炉1に挿入する。炉頂からは同時に石灰石
及びコークスを挿入する。羽口2からは熱風を吹
込む。更に炉中段3から予熱ガスを吹込む。予熱
ガスは炉頂ガスの一部をバーナーに導入してこれ
を燃焼することにより得られ、その温度は約500
℃〜1300℃である。予熱ガスは、鉱石中に含まれ
る多量の水分の蒸発を助けるために行う。
このような操業によりフエロニツケル鉱石の還
元が進行し、炉底部でFeNi及びスラグが得られ
る。
この方法によれば、炉中段から予熱ガスを吹込
んでいるので鉱石に含まれる多量の水分の蒸発を
促進し、コークス比を減少することができる。し
かもボツシユガス量を下げて生産性を向上するこ
とができ、高炉によるフエロニツケル製造の操業
を安定して行なうことができる。
次に本発明の高炉操業における物質及び熱収支
につき説明する。
その計算条件を表1に示す。
(Industrial Application Field) The present invention relates to a method for producing ferronic acid using a blast furnace. (Prior art and its problems) Nickel raw material ore has a low grade of about 2% nickel, and a large amount of adhering water and crystallization water, about 30%, and usually requires preliminary treatment such as drying and pelletizing. Conventionally, nickel ore has been generally produced by reducing it in a kiln or shaft furnace and melting it in an electric furnace, and methods using blast furnaces have only been partially used. However, when a blast furnace is used, since there is a lot of water in the raw material of Ferronickel, a lot of fuel is consumed to evaporate the water, resulting in problems such as an increase in the coke ratio, an increase in the furnace top temperature, and a decrease in productivity. (Technical Problems to be Solved by the Invention) An object of the present invention is to provide a method for producing ferronic acid that can lower the coke ratio, lower the furnace top gas temperature, and improve productivity. (Means for Solving Technical Problems) The present invention provides a method for producing ferronic acid, which is characterized in that ferronic acid ore is inserted from the upper part of the furnace, hot air is blown from the tuyere, and preheated gas is blown from the shaft section in the middle of the furnace. It is. (Example) Examples of the present invention will be described below with reference to the drawings. As shown in Figure 1, nickel ore is sieved after drying, lump ore is directly inserted from the top of blast furnace 1, and fine ore is granulated and inserted into blast furnace 1 as green balls, or after granulation. Insert into blast furnace 1 as a cold bond. Limestone and coke are simultaneously inserted from the top of the furnace. Hot air is blown from tuyere 2. Furthermore, preheating gas is blown from the middle stage 3 of the furnace. Preheating gas is obtained by introducing a part of the furnace top gas into a burner and burning it, and its temperature is approximately 500℃.
℃~1300℃. Preheating gas is performed to help evaporate a large amount of water contained in the ore. Through such operations, reduction of ferronite ore progresses, and FeNi and slag are obtained at the bottom of the furnace. According to this method, since the preheating gas is blown from the middle stage of the furnace, the evaporation of a large amount of water contained in the ore can be promoted and the coke ratio can be reduced. In addition, productivity can be improved by reducing the amount of boiling gas, and the operation of producing ferronic acid using a blast furnace can be carried out stably. Next, the material and heat balance in the blast furnace operation of the present invention will be explained. Table 1 shows the calculation conditions.
【表】
計算結果を第2図及び第3図に示す。第2図は
熱線図で、この図からフエロニツケル鉱石の場
合、スラグ量が過大で(約7000Kg/T)、その持
出し顕熱が大きいが鉱石水分の蒸発潜熱が非常に
大きく、炉下部よりも炉上部で熱が不足気味で燃
料比が高くなつている。コークス比CRを2500
Kg/Tから1500Kg/Tとすると、予熱ガスを吹込
まない比較例の場合は炉上部で熱不足となる。し
かし実施例の方法では、1000℃の予熱ガスを吹込
んでいるので、コークス比を1500Kg/Tと下げて
も熱不足を解消できる。第3図は炉頂ガス温度と
コークス比の関係を示す。この図から、コークス
比を下げると炉頂温度が著しく低下し、予熱ガス
の吹き込みが必要であることがわかる。
また表2は主要な原単位の項目と熱収支、ガス
量を示す。[Table] The calculation results are shown in Figures 2 and 3. Figure 2 is a heat diagram. This figure shows that in the case of ferronic ore, the amount of slag is excessive (approximately 7000Kg/T), and the sensible heat taken out is large, but the latent heat of vaporization of ore moisture is very large, and the furnace is lower than the lower part of the furnace. There seems to be a lack of heat at the top, and the fuel ratio is high. Coke ratio CR 2500
When changing from Kg/T to 1500 Kg/T, in the case of the comparative example in which no preheating gas is blown, there is a lack of heat in the upper part of the furnace. However, in the method of the embodiment, since preheated gas at 1000°C is blown, the heat deficiency can be overcome even if the coke ratio is lowered to 1500 kg/T. Figure 3 shows the relationship between furnace top gas temperature and coke ratio. From this figure, it can be seen that when the coke ratio is lowered, the furnace top temperature drops significantly, making it necessary to blow preheating gas. Table 2 shows the main unit consumption items, heat balance, and gas amount.
【表】【table】
【表】
*循環ガスを除く
表2から、水分の蒸発に必要とするエネルギー
を羽口先からのガスで満たそうとすると(比較方
法)、必要ボツシユガス量、即ち燃料比FRが高く
なる。燃料比FRが高くなると排ガス潜熱が大き
くなり、所要熱量が増加する。本実施例では、予
熱ガスを吹込むことにより、低い温度レベルのガ
スを多量に吹込むことにより熱収支を満たしてい
る。即ち、実施例では燃料比が低いのでボツシユ
ガス量を低くできることがわかる。フエロニツケ
ル鉱石はスラグ量が非常に多く<フラツデイング
限界に近いので、ボツシユガス量を低くすること
により、生産性を上げることができる。
(発明の効果)
本発明によれば、炉中段から予熱ガスを吹込ん
でいるので、水分の蒸発を助け、コークス比を減
少し、炉頂ガス温度を下げ、ボツシユガス量を下
げて、生産性の向上及び操業の安定を図ることが
できる。[Table] *Excluding circulating gas From Table 2, if you try to fill the energy required for water evaporation with gas from the tuyere tip (comparison method), the required amount of boiling gas, that is, the fuel ratio FR will increase. As the fuel ratio FR increases, the exhaust gas latent heat increases and the required amount of heat increases. In this embodiment, the heat balance is satisfied by blowing in a large amount of gas at a low temperature level by blowing in preheated gas. That is, it can be seen that in the example, since the fuel ratio is low, the amount of boiling gas can be reduced. Since ferronite ore has a very large amount of slag and is close to the flattening limit, productivity can be increased by lowering the amount of slag gas. (Effects of the Invention) According to the present invention, since preheating gas is injected from the middle stage of the furnace, it helps the evaporation of moisture, reduces the coke ratio, lowers the furnace top gas temperature, and lowers the amount of boiling gas, thereby improving productivity. It is possible to improve the efficiency and stabilize operations.
第1図は本発明の一実施例を示す高炉操業方法
の説明図、第2図は温度と熱量との関係を示す
図、第3図は炉頂温度とコークス比との関係を示
す図である。
1…高炉、2…羽口、3…炉中段。
Fig. 1 is an explanatory diagram of a blast furnace operating method showing an embodiment of the present invention, Fig. 2 is a diagram showing the relationship between temperature and amount of heat, and Fig. 3 is a diagram showing the relationship between furnace top temperature and coke ratio. be. 1... Blast furnace, 2... Tuyere, 3... Middle stage of the furnace.
Claims (1)
熱風を吹込むとともに炉中段のシヤフト部から予
熱ガスを吹込むことを特徴とするフエロニツケル
の製造方法。1. A method for producing ferro-nickel, which comprises inserting nickel ore from the upper part of the furnace, blowing hot air through the tuyeres, and blowing preheated gas through the shaft section in the middle of the furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13462386A JPS62290842A (en) | 1986-06-10 | 1986-06-10 | Manufacture of ferronickel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13462386A JPS62290842A (en) | 1986-06-10 | 1986-06-10 | Manufacture of ferronickel |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62290842A JPS62290842A (en) | 1987-12-17 |
JPH0430455B2 true JPH0430455B2 (en) | 1992-05-21 |
Family
ID=15132703
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13462386A Granted JPS62290842A (en) | 1986-06-10 | 1986-06-10 | Manufacture of ferronickel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62290842A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1300352C (en) * | 2005-09-16 | 2007-02-14 | 刘沈杰 | Nickel-iron smelting process from nickel oxide ore containing crystal water through blast furnace |
CN1306049C (en) * | 2005-09-16 | 2007-03-21 | 刘沈杰 | Ferronickel smelting process of nickel oxide ore free of crystal water in blast furnace |
JP5991290B2 (en) * | 2013-09-13 | 2016-09-14 | Jfeスチール株式会社 | Method for producing sintered ore |
-
1986
- 1986-06-10 JP JP13462386A patent/JPS62290842A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS62290842A (en) | 1987-12-17 |
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