JPS61223137A - Sintering operation method utilizing crude graphite - Google Patents

Sintering operation method utilizing crude graphite

Info

Publication number
JPS61223137A
JPS61223137A JP6556585A JP6556585A JPS61223137A JP S61223137 A JPS61223137 A JP S61223137A JP 6556585 A JP6556585 A JP 6556585A JP 6556585 A JP6556585 A JP 6556585A JP S61223137 A JPS61223137 A JP S61223137A
Authority
JP
Japan
Prior art keywords
sintering
graphite
blast furnace
starting materials
crude graphite
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
Application number
JP6556585A
Other languages
Japanese (ja)
Inventor
Shigenori Uno
宇野 成紀
Yukio Umetsu
梅津 幸雄
Junichi Kodama
順一 児玉
Shigehisa Kata
加太 茂久
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP6556585A priority Critical patent/JPS61223137A/en
Publication of JPS61223137A publication Critical patent/JPS61223137A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain high thermal efficiency by kneading crude graphite produced from molten pig iron in a blast furnace with finely powdered starting materials and using the kneaded material as primary fuel for sintering in place of nearly equivalent coke breeze. CONSTITUTION:Unrefined crude graphite (a) produced from molten pig iron in a blast furnace is kneaded with dusts (b) as finely powdered starting materials in a kneader 1 after the water content is regulated to about 9%, and the kneaded material is sent to an ore storage tank 2 as primary fuel for sintering. This primary fuel is mixed with ore, secondary starting materials and coke breeze in primary and secondary mixers 3, 4, and the mixture is fed to a pallet carriage 5 as a starting material to be sintered in the form of granules. Thus, the consumption unit of coke breeze can be reduced.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、高炉溶銑の鋳鉄時に発生する粗グラファイト
を焼結用原燃料として利用する焼結操業方法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a sintering operation method that utilizes crude graphite generated during the casting of hot metal in a blast furnace as raw fuel for sintering.

(従来の技術、問題点) 高炉溶銑の鋳銑時に発生するグラファイトは。(Conventional technology, problems) Graphite is generated during the casting of blast furnace hot metal.

カー g ンO(D他ニpe、 sio、、 cao等
の不純物が多く、0のみ回収してC品位を上げて電極な
どの化学原料として用いることが考えられるが、0品位
を上げるには浮選等の精製処理工程を経る必要、があシ
、処理コストがかかる等コスト上の問題があり、実用化
には至っていなかった。
There are many impurities such as carbon O (D, nipe, sio, cao, etc.), and it is possible to collect only 0 and improve the C grade and use it as a chemical raw material for electrodes, etc., but in order to increase the 0 grade, it is necessary to It has not been put into practical use because of cost problems such as the need to go through purification processes such as screening, oxidation, and high processing costs.

一方、従来0を含んだ焼結用原燃料として高炉1火入、
焼結ダスト、転炉ダスト等の製鉄の各工程で発生するダ
ストが用いられてきたが、高炉灰00品位はせいぜい3
5%程度であ夛、原燃料として使用したとしてもその効
果は小さく、通常の粉コークスにKらべると、その熱効
率は70%程度であった。
On the other hand, conventionally, one blast furnace was fired as raw fuel for sintering containing 0,
Dust generated in each process of steelmaking, such as sintering dust and converter dust, has been used, but blast furnace ash 00 grade is at most 3.
Even when used as a raw fuel at a concentration of about 5%, the effect is small, and when compared to ordinary coke breeze, its thermal efficiency was about 70%.

これより、0品位が高い粗グラファイトの利用が検討さ
れてきたが、粗グラファイトは非常に微粉であるために
ハンドリング時の飛散が問題とな)、水分t−添加して
飛散を防止するためには25%程度の水分とする仁とが
必要であり粗グラファイト単味で焼結用原燃料として使
用した場合は貯鉱槽内で積重が発生し、焼結の工程変動
を大きくする等問題があり、実用化までは至っていなか
った。
From this, the use of coarse graphite with a high zero grade has been considered, but since coarse graphite is a very fine powder, scattering during handling is a problem), so it is necessary to add water to prevent scattering. It is necessary to have grains with a moisture content of about 25%, and if crude graphite alone is used as raw material and fuel for sintering, it will cause problems such as stacking in the storage tank and increasing fluctuations in the sintering process. However, it had not yet been put into practical use.

本発明は、このような問題点を解決した。高炉溶銑の鋳
銑時に発生する粗グラフアイ)1−焼結用原燃料として
利用する方法1に提供する。
The present invention has solved these problems. Rough graphite generated during casting of blast furnace hot metal) 1) Provided in method 1 for use as raw fuel for sintering.

(問題点t−解決するための手段、作用)本発明は、高
炉溶銑から発生する未精製の粗グラファイトを微粒原料
と混練して焼結用原燃料として使用することを特徴とす
る焼結操業方法である。
(Problem t-Means and effects for solving) The present invention is a sintering operation characterized in that unrefined coarse graphite generated from blast furnace hot metal is kneaded with fine grain raw material and used as raw fuel for sintering. It's a method.

なお、本発明において微粒原料とは平均粒度が0.5園
以下の焼結用原料を指し、鉄を含有するものである。
In the present invention, the fine grain raw material refers to a raw material for sintering having an average particle size of 0.5 mm or less, and contains iron.

本発明者は、上記問題に鑑み、粗グラファイトの焼結用
原燃料としての使用方法′fr種々検討した結果、高炉
1火入、その他のダスト等の微粒焼結用原料と事前に7
レツドミキサー、あるいはアイ1    リツヒミキサ
ー等の混線機で混練することにより。
In view of the above-mentioned problems, the inventor of the present invention has investigated various ways of using crude graphite as a raw material fuel for sintering.
By kneading with a mixer such as a Red mixer or an I1 Rich mixer.

粗グラファイトのハンドリング辱に発生する飛散等の問
題もなく使用でき、燃料としての効果もダストに比べて
高く、はぼ粉コークスと等価で置換できることを確認し
次。
It has been confirmed that it can be used without the problems of scattering that occur when handling coarse graphite, is more effective as a fuel than dust, and can be equivalently replaced with powdered coke.

また、特願昭58−145887号に提案されているよ
うに、事前混合した原料を焼結点火炉前の焼結ベッド上
表層に散布する仁とによシ焼結上層の冷間強度が改善さ
れ、歩留シが向上することも確認した。
In addition, as proposed in Japanese Patent Application No. 145887/1987, the cold strength of the upper layer of sintering is improved by spreading pre-mixed raw materials on the surface layer of the sintering bed in front of the sintering ignition furnace. It was also confirmed that the yield was improved.

(実施例) 次に、実施例に基づいて本発明の詳細な説明する。(Example) Next, the present invention will be explained in detail based on examples.

〔実施例1〕 実施例1は、粗グラファイトを他の鉄鉱石および造滓原
料と事前に混線、造粒して焼結用原燃料として使用した
場合である。
[Example 1] Example 1 is a case where crude graphite is mixed and granulated with other iron ore and slag raw material in advance and used as raw fuel for sintering.

本1j!施例は、焼結面積170−のDL式廃結機で行
なったもので、第1表に粗グラファイトおよび微粒原料
の配合比、ならびに粗グラファイト使用時のC品位の変
化例を示した。@iグラファイト以外は機料原料である
。グラファイトは最大50%まで配合可能であつ友。
Book 1j! The examples were carried out using a DL type waste machine with a sintering area of 170 mm, and Table 1 shows examples of changes in the blending ratio of coarse graphite and fine grain raw materials and the C grade when coarse graphite is used. @iOther than graphite are raw materials. Graphite can be added up to 50% and is a good friend.

第   1   表 第2表に高炉灰および粗グラファイトの代表成分を示し
九、  第 2 表 第3表には焼結原料配合比を示した。粗グラファイトは
全体の0.4%とわずかである。
Tables 1 and 2 show the representative components of blast furnace ash and crude graphite, and Tables 2 and 3 show the sintering raw material blending ratios. Crude graphite is only 0.4% of the total.

嬉3表 粗グラファイトaは、第1図に示したように微粒原料で
あるダスト類すとともに混練機IKて水分9XIC調整
して混練し、これを焼結用原燃料として焼結貯鉱槽2に
送プ、他の鉱石、副原料および粉コークスとともに1次
ミキサー3.2次ミキサー4で混合、造粒し、焼結原料
としてパレット台車5上に装入した。
As shown in Fig. 1, coarse graphite a is mixed with dust, which is a fine raw material, in a kneader IK with a moisture content adjusted to 9XIC, and this is used as raw fuel for sintering in the sintering ore storage tank 2. It was mixed with other ores, auxiliary raw materials and coke powder in a primary mixer 3 and a secondary mixer 4, granulated, and charged onto a pallet truck 5 as a sintering raw material.

第2図に粗グラファイトを配合原料中0.4%使用した
試験時の歩留、 Fed、コークス配合比の推移を示し
た。
Figure 2 shows the changes in yield, Fed, and coke blending ratio during a test in which 0.4% of crude graphite was used in the blended raw materials.

・    これより1歩留り一定で粗グラファイト、の
0の増加に等しいコークス配合比の低減が図られ、0置
換率はほぼ100%であった。
- From this, it was possible to reduce the coke blending ratio equivalent to a zero increase in crude graphite at a constant yield, and the zero substitution rate was almost 100%.

この結果、第3図に示したように本発明法により粉コー
クス原単位が低減できた。
As a result, as shown in FIG. 3, the method of the present invention was able to reduce the basic unit of coke breeze.

〔実施例2〕 実施例2は、第4図に示したように事前に粗グラファイ
トと微粒原料であるダスト類を混練した焼結用原燃料を
点火前に焼結ベッド表層に散布した例である。粗グラフ
ァイトを混練また原料ct−ホッノぐ−6に装入し、こ
れより定量切出し装置7により一定量切出し、ベッド巾
方向に原料を拡散する散布板8によりノぐレット巾方向
に均一に散布した後に点火炉9内でOOGを燃料とした
バーナー10により着火し念。
[Example 2] Example 2 is an example in which raw fuel for sintering, which was prepared by kneading coarse graphite and dust, which is a fine raw material, was sprinkled on the surface layer of the sintering bed before ignition, as shown in Fig. 4. be. Crude graphite was kneaded and charged into a raw material ct-hog hole 6, from which a fixed amount was cut out using a quantitative cutting device 7 and uniformly spread in the width direction of the hole using a scattering plate 8 that spread the raw material in the width direction of the bed. Later, it was ignited in the ignition furnace 9 by the burner 10 using OOG as fuel.

ここで使用した粗グラファイトを混練した原燃料Cは第
1表および第2表に示した配合および性状のものンした
。この結果、C品位11.3%の粗グラファイト(粉コ
ークス1 kg/ t−sと0量等価)を混練した焼結
用原燃料を7.5 Sct/ t−s  散布すること
により、第5図に示したようICm結ベッド表層の冷間
強度が10%改善され、第6図に示し九ように歩留りが
1.4%改善された。また、第7図に示したようにOO
G原単位も0.5 Nd/ t−8低減できた。
The raw fuel C obtained by kneading crude graphite used here had the composition and properties shown in Tables 1 and 2. As a result, by spraying 7.5 Sct/t-s of raw fuel for sintering mixed with crude graphite with a C grade of 11.3% (equivalent to 1 kg/t-s of coke powder), the fifth As shown in the figure, the cold strength of the surface layer of the ICm bed was improved by 10%, and as shown in Figure 6, the yield was improved by 1.4%. Also, as shown in Figure 7, OO
The G consumption rate was also reduced by 0.5 Nd/t-8.

第  4  表 本実施例と粉コークスのみを散布した場合の効果を比較
すると第4表のごとくなり、本実施例はCソースが他原
料と混合されているため着火性が低下してOOG原単位
の改善式が小さくなっているが、鉄を多く含む原料を使
用する丸め高温状態で長時間保持され、歩留)改善効果
が大t!!it’ a粉コークス単味散布に比較して本
実施例におけるコスト低減は大きく、さらに0ソースと
して安価な粗グラファイトを用いるため、より大きなコ
スト低減が図れる。
Table 4 Comparing the effects of this example and the case of spraying only coke powder, the results are as shown in Table 4. In this example, the C source is mixed with other raw materials, so the ignitability is reduced and the OOG consumption rate is lower. Although the improvement formula is smaller, the improvement effect (yield) is large because the rolling material using iron-rich raw materials is kept at high temperatures for a long time! ! The cost reduction in this example is greater than that in the case of single sprinkling of coke powder, and furthermore, since inexpensive crude graphite is used as the zero source, even greater cost reduction can be achieved.

(発明の効果) 以上のように、粗グ27アイトを平均粒度0.5箇以下
の微粒原料と混練して焼結用原燃料として使用すること
により、粉コークスと1:1の置換が可能であり、高い
熱効率を有することを確認した。
(Effect of the invention) As described above, by kneading coarse 27ite with fine raw material with an average particle size of 0.5 particles or less and using it as a raw fuel for sintering, it is possible to replace coke powder on a 1:1 basis. It was confirmed that it has high thermal efficiency.

また、粗グラファイトを平均粒度0.5m以下の微粒原
料と混練した焼結用原燃料を焼結ベッド表層に散布する
仁とにより、ベッド表層の歩留りおよび点火用のコーク
スガスの節減が図られた。
In addition, by spraying the raw fuel for sintering, which is made by kneading coarse graphite with a fine raw material with an average particle size of 0.5 m or less, on the surface layer of the sintering bed, the yield of the bed surface layer and the consumption of coke gas for ignition were reduced. .

従って、本発明は焼結鉱のコストダウンに寄与するとこ
ろ極めて大である。
Therefore, the present invention greatly contributes to reducing the cost of sintered ore.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の詳細な説明する図、 第2図は歩留、Fed、コークス配合比の推移を示す図
。 第3図は粉コークス原単位低減効果を示す図。 第4図は本発明の他の実施例を示す図、第5図は焼結ベ
ッド表層の冷間強度改善効果を示す図、 第6図は歩留り改善効果を示す図、 第7図はOOG原単位低減効果を示す因である。 l・・・混練機、2・・・焼結貯鉱槽、3・・・1次ミ
キサー、4・・・2次ミキサー、5・・・パレット台車
、6・・・ホッパー、7・・・定量切出し装置、8・・
・散布板、9・・・点火炉、10・・・バーナー。 代理人 弁理士 秋 沢 政 光 他2名 ff3図 茸4図 アフロ 自発手続補正書 昭和60年4月30日 り許庁氏宮殿 事件の表示 特願昭60−65565号 発明の名称 粗グラファイト利用焼結操業方法 、補正をする者 事件との関係  出 願 人 住    所 東京都千代田区大手町2丁目6番3号名
    称 (665)新日本製鐵株式会社、代理人
FIG. 1 is a diagram explaining the present invention in detail, and FIG. 2 is a diagram showing changes in yield, Fed, and coke blending ratio. Figure 3 is a diagram showing the effect of reducing coke powder consumption per unit. Fig. 4 shows another embodiment of the present invention, Fig. 5 shows the cold strength improvement effect of the surface layer of the sintered bed, Fig. 6 shows the yield improvement effect, and Fig. 7 shows the OOG raw material. This is the cause of the unit reduction effect. l...kneader, 2...sintered ore storage tank, 3...primary mixer, 4...secondary mixer, 5...pallet truck, 6...hopper, 7... Quantitative cutting device, 8...
- Spreading plate, 9... Ignition furnace, 10... Burner. Agent Patent Attorney Masamitsu Aki Sawa and 2 others ff 3 Mushroom 4 Afro Voluntary Procedure Amendment April 30, 1985 Indication Patent Application No. 1987-65565 for the Licensed Agency Ushinomiya Case Name of the Invention: Coarse graphite utilization firing Relationship with the case of the person making the amendment Application Address 2-6-3 Otemachi, Chiyoda-ku, Tokyo Name (665) Nippon Steel Corporation, Agent

Claims (1)

【特許請求の範囲】[Claims] (1)高炉溶銑から発生する未精製の粗グラファイトを
微粒原料と混練して焼結用原燃料として使用することを
特徴とする焼結操業方法。
(1) A sintering operation method characterized in that unrefined coarse graphite generated from blast furnace hot metal is kneaded with fine grain raw material and used as raw fuel for sintering.
JP6556585A 1985-03-29 1985-03-29 Sintering operation method utilizing crude graphite Pending JPS61223137A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6556585A JPS61223137A (en) 1985-03-29 1985-03-29 Sintering operation method utilizing crude graphite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6556585A JPS61223137A (en) 1985-03-29 1985-03-29 Sintering operation method utilizing crude graphite

Publications (1)

Publication Number Publication Date
JPS61223137A true JPS61223137A (en) 1986-10-03

Family

ID=13290660

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6556585A Pending JPS61223137A (en) 1985-03-29 1985-03-29 Sintering operation method utilizing crude graphite

Country Status (1)

Country Link
JP (1) JPS61223137A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS562134A (en) * 1979-06-19 1981-01-10 Toshiba Corp Molding method for roll of bellows

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS562134A (en) * 1979-06-19 1981-01-10 Toshiba Corp Molding method for roll of bellows

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