JP2004076148A - Steelmaking raw materials - Google Patents
Steelmaking raw materials Download PDFInfo
- Publication number
- JP2004076148A JP2004076148A JP2002272266A JP2002272266A JP2004076148A JP 2004076148 A JP2004076148 A JP 2004076148A JP 2002272266 A JP2002272266 A JP 2002272266A JP 2002272266 A JP2002272266 A JP 2002272266A JP 2004076148 A JP2004076148 A JP 2004076148A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- collected
- dust
- coke
- binder
- 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
Images
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
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】
【発明の属する技術分野】
製鉄所内製鋼工場にある転炉より発生し集塵機にて捕集されたダストと同じく製鉄所内にあるコークス炉より発生し集塵機にて捕集されたコークス粉をバインダーと共にミキサーに入れ十分混練したのち、プレス機を用いて成型した鉄原料に関するものである。
より詳しくは、リン、イオウおよび重金属などの不純物を含まず、且つ一定形状のためハンドリングが容易な電気炉製鋼および鋳物製造に適した安価で且つ良質な製鉄原料である。
【0002】
【従来の技術】
転炉での脱炭時、大量に発生する排ガスは従来と異なり殆どがガス回収方式となっているため、捕集されるダストも粒子の表面がわずかに酸化されるのみで大部分がメタリック鉄の形態を保っている。
しかしながら集塵ダストは数mm.あるいはそれ以下の微粉であり、しかも通常ベンチュリースクラバーにて捕集・回収される為、20%程度の水分を保有している。
従って一部が鉄原料として転炉に還元され、また電気炉製鋼用原料として使用されてはいるものの微粉である為ハンドリング時にロスが生じること、また炉内溶解途中において、空気中の酸素にて酸化されスラグになってしまうなどの問題がある。
従って大半のダストは製鉄所内の焼結工場に持込み焼結鉱となし、鉄鉱石の代替品として高炉に還元されているのが実情である。
【0003】
【発明が解決しようとする課題】
以上述べてきた如く不純物が少なく良質な鉄源であるにも拘らず、微粉であるがゆえに、有効なリサイクル方法が確立していない。
特に焼結工場にて焼結し高炉に戻す従来法は、ダスト中の折角のメタリック鉄を焼結工程で酸化し酸化鉄となし、それを高炉にて再度メタリック鉄に還元するという二重の無駄をしていることになる。
そこでダスト表面を覆う酸化鉄を還元するに必要なカーボンを配合し振動プレス機などで成型して、ハンドリングおよび溶解時にロスの発生しない良質な鉄原料を提案するものである。
【0004】
【発明を解決するための手段】
まず集塵機により捕集されたダストをロータリードライヤー等の乾燥機を用いて乾燥する。しかし後工程にてセメントなどのバインダーを混合する際、水を添加するためダスト中に若干の水分が残留することは全く問題ない。
乾燥後のダストは必要あらばコークス炉からの集塵コークス粉とセメントおよび/または澱粉と共にミキサーに入れられ十分に混合される。
集塵コークスの配合量はダスト中の酸化鉄を還元するに要する理論量の1.50倍以下が望ましい。カーボンは製鋼時あるいは鋳物製造時不可欠な元素であるため配合量が多すぎても特に問題になることはない。
しかし、多すぎると成型が難しくなり充分な成型強度が得られないこともあるため配合量を制限した。
次にバインダーであるがセメントもしくは澱粉あるいはその混合物が望ましい。何故なら、安価である上、自然養生でも充分な強度を得ることが出来るからである。
又、バインダー等の添加物は成型物の鉄含有量を希釈し、且つスラグの生成量を増やすことから出来るだけ少量におさえるべきである。具体的にはダストの粒子形状、サイズ等の性状により変動するが数パーセントより10%未満が望ましい。
【0005】
ミキサーより排出された混合物は直ちに振動プレス機にかけられ成型される。成型物は溶解に支障を来たさない大きさであれば問題ないが、大きすぎると強度が出ず、また養生にも時間がかかる。
一方、小さすぎても成型の生産性が悪くなるため一個あたりの重量が1キログラムから10キログラムがベストである。
また、形状は問わないがハンドリング中に破損しにくい丸みをおびた形状が望ましい。
【0006】
成型物は養生を行うことにより強度を増すことが出来る。養生は屋内に放置するいわゆる自然養生でも構わないが、時間がかかるため大きなスペースを必要とする。時間とスペースを減らすためにバンドドライヤータイプの養生機を使用することも有効である。
養生の完了した成型物は屋内に保管され、必要に応じてマグネットもしくはショベルカーを使用しトラックに積み込み出荷される。
【0007】
【発明の実施の形態】
以下、この発明を実施例を用いて具体的に説明する。
今回のテストに使用した転炉集塵ダストの成分分析値を表−1に示す。
【表−1】
又、使用したコークス炉集塵粉、即ちコークス微粉の成分分析値を表−2に示す。
【表−2】
なお、バインダーとして使用したセメントは通常のポルトランドセメントを使用した。又、スラグの流動性を改善するために少量の蛍石を使用することとした。
【0008】
【実施例】
前述の各材料を以下の割合で配合し、簡易ミキサーで充分混練した。
集塵ダスト ;500kg
コークス粉 ; 20kg
セメント ; 50kg
蛍石 ; 5kg
混練後、直ちに振動プレス機にて成型を行った。なお金型は約800CCのものを使用した。
50個の正常な成型物を製造したが、平均単重は3.5kgであった。
【0009】
次に溶解歩留まりを確認するために、100kgの高周波誘導炉を用いて3回の溶解試験を行った。一回当たりの成型物の装入量は20個とした。
完全に溶解し約30分保持したのち、電源を切りそのまま冷却した。凝固後メタルを取り出し重量を測定した。
各々のメタル量は52.7kg、54.0kg、51.2kgであり平均の鉄歩留まりは94.7%であった。
【0010】
【発明の効果】
かくしてこの発明によれば、転炉集塵ダストを必要あらば同じく製鉄所にて副生しているコークス粉と共に成型することにより、ハンドリングが容易で、且つ溶解歩留まりの優れた良質な鉄原料を得ることが出来る。
【図面の簡単な説明】
【図1】この発明の製造工程を示す図である。
【符号の説明】
1.乾燥炉
2.ミキサー
3.プレス機
4.養生炉[0001]
TECHNICAL FIELD OF THE INVENTION
After the coke powder generated from the coke oven in the steelworks and collected by the dust collector as well as the dust generated from the converter in the steelworks in the steelworks and collected by the dust collector, was put into a mixer together with the binder and kneaded well, The present invention relates to an iron raw material formed using a press machine.
More specifically, it is an inexpensive and high-quality raw material suitable for electric furnace steelmaking and casting production that does not contain impurities such as phosphorus, sulfur, and heavy metals and has a uniform shape and is easy to handle.
[0002]
[Prior art]
Exhaust gas generated in large quantities during decarburization in a converter is a gas recovery system, unlike the conventional method. Therefore, most of the collected dust is only slightly oxidized on the surface of the particles and metallic iron The form is maintained.
However, the dust collected is several mm. Or, it is fine powder smaller than that, and since it is usually collected and collected by a venturi scrubber, it has about 20% moisture.
Therefore, a part is reduced to the converter as iron raw material, and although it is used as a raw material for electric furnace steelmaking, it is a fine powder, causing a loss at the time of handling. There are problems such as oxidation and slag.
Therefore, most of the dust is brought into the sintering plant in the steel mill and converted into sinter, and is reduced to the blast furnace as a substitute for iron ore.
[0003]
[Problems to be solved by the invention]
As described above, an effective recycling method has not been established because of the fine powder despite the fact that it is a good quality iron source with few impurities.
In particular, the conventional method of sintering in a sintering plant and returning to the blast furnace is a double method of oxidizing the metallic iron in the dust in the sintering process into iron oxide and reducing it to metallic iron again in the blast furnace. You are wasting.
Therefore, the present invention proposes a high-quality iron raw material that does not cause loss during handling and melting by blending carbon necessary for reducing iron oxide covering the dust surface and molding it with a vibration press or the like.
[0004]
[Means for Solving the Invention]
First, the dust collected by the dust collector is dried using a dryer such as a rotary dryer. However, when a binder such as cement is mixed in a later step, since water is added, there is no problem that a small amount of water remains in the dust.
The dust after drying is put into a mixer together with dust and coke dust from a coke oven and cement and / or starch, if necessary, and mixed well.
The mixing amount of the dust collecting coke is desirably 1.50 times or less the theoretical amount required for reducing iron oxide in the dust. Carbon is an indispensable element at the time of steel making or casting production, so that there is no particular problem even if the compounding amount is too large.
However, if the amount is too large, molding is difficult and sufficient molding strength may not be obtained, so that the blending amount is limited.
Next, as a binder, cement or starch or a mixture thereof is desirable. This is because it is inexpensive and can obtain sufficient strength even with natural curing.
Further, additives such as a binder should be kept as small as possible in order to dilute the iron content of the molded product and increase the amount of slag produced. Specifically, it varies depending on the properties such as the particle shape and size of the dust, but is desirably from several percent to less than 10%.
[0005]
The mixture discharged from the mixer is immediately applied to a vibrating press and molded. There is no problem if the molded product has a size that does not hinder the dissolution, but if it is too large, strength is not obtained and curing takes time.
On the other hand, if the size is too small, the productivity of molding is deteriorated, so that the weight per piece is preferably 1 to 10 kg.
The shape is not limited, but a rounded shape that is not easily damaged during handling is desirable.
[0006]
The molded product can be strengthened by curing. The curing may be a so-called natural curing that is left indoors, but requires a large space because it takes time. It is also effective to use a band dryer type curing machine to reduce time and space.
The cured moldings are stored indoors, and loaded onto trucks using magnets or shovels as necessary.
[0007]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be specifically described with reference to examples.
Table 1 shows the component analysis values of the converter dust collected in this test.
[Table-1]
Table 2 shows the component analysis values of the used coke oven dust, that is, the coke fines.
[Table-2]
Note that ordinary Portland cement was used as the cement used as the binder. In addition, a small amount of fluorite was used to improve the fluidity of the slag.
[0008]
【Example】
Each of the above-mentioned materials was blended in the following ratio and kneaded sufficiently with a simple mixer.
Dust collected; 500 kg
Coke powder; 20kg
Cement; 50kg
Fluorite; 5kg
Immediately after kneading, molding was performed using a vibration press. The die used was about 800 CC.
Fifty normal moldings were produced, but the average unit weight was 3.5 kg.
[0009]
Next, in order to confirm the melting yield, a melting test was performed three times using a 100 kg high-frequency induction furnace. The charging amount of the molded product at one time was 20 pieces.
After completely dissolving and holding for about 30 minutes, the power was turned off and the system was cooled as it was. After solidification, the metal was taken out and its weight was measured.
The amount of each metal was 52.7 kg, 54.0 kg, and 51.2 kg, and the average iron yield was 94.7%.
[0010]
【The invention's effect】
Thus, according to the present invention, if necessary, the dust collected from the converter is molded together with coke powder by-produced at the steel mill as well, so that a high-quality iron raw material that is easy to handle and has an excellent melting yield can be obtained. Can be obtained.
[Brief description of the drawings]
FIG. 1 is a diagram showing a manufacturing process of the present invention.
[Explanation of symbols]
1. Drying oven2.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002272266A JP2004076148A (en) | 2002-08-15 | 2002-08-15 | Steelmaking raw materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002272266A JP2004076148A (en) | 2002-08-15 | 2002-08-15 | Steelmaking raw materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2004076148A true JP2004076148A (en) | 2004-03-11 |
Family
ID=32024905
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2002272266A Pending JP2004076148A (en) | 2002-08-15 | 2002-08-15 | Steelmaking raw materials |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2004076148A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005087956A1 (en) * | 2004-03-12 | 2005-09-22 | Jtekt Corporation | Briquette for raw material of metal and method for production thereof |
| WO2009017059A1 (en) * | 2007-07-27 | 2009-02-05 | Kabushiki Kaisha Kobe Seiko Sho | Process for producing carbonaceous-material-including metal oxide briquet |
-
2002
- 2002-08-15 JP JP2002272266A patent/JP2004076148A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005087956A1 (en) * | 2004-03-12 | 2005-09-22 | Jtekt Corporation | Briquette for raw material of metal and method for production thereof |
| WO2009017059A1 (en) * | 2007-07-27 | 2009-02-05 | Kabushiki Kaisha Kobe Seiko Sho | Process for producing carbonaceous-material-including metal oxide briquet |
| US8206487B2 (en) | 2007-07-27 | 2012-06-26 | Kobe Steel, Ltd. | Method for producing carbon composite metal oxide briquettes |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101302578B (en) | A kind of composite vanadium extraction and dephosphorization agent for vanadium-containing molten iron and preparation method thereof | |
| JP2003073722A (en) | Method for manufacturing granular metal | |
| CN101333089A (en) | Process for producing MgO-C Bricks by using waste MgO-C Bricks as main raw material | |
| CN104131130B (en) | Converter final slag modifier and application thereof | |
| CN110079665A (en) | A kind of preparation method of the high-carbon metallized pellet for electric furnace | |
| JPH06145836A (en) | Production of alloy utilizing aluminum slag | |
| CN103088186B (en) | Slag-making method for rapid dephosphorization of semisteel | |
| JP2009149984A (en) | Method for manufacturing nickel cold pig iron by using nickel ore and formed article of stainless steel by-product | |
| JP2004076148A (en) | Steelmaking raw materials | |
| CN107365161B (en) | Copper composite magnesia-chrome brick and manufacturing method thereof | |
| JP5332806B2 (en) | Electric furnace dust recycling method | |
| JP4540488B2 (en) | Desulfurization method of ferronickel | |
| JP6071409B2 (en) | Pre-granulation method for sintering raw materials | |
| JP5558119B2 (en) | How to use granular iron | |
| JP2002241853A (en) | Unfired agglomerate for blast furnace | |
| KR20120072576A (en) | A method of manufacturing composite pellet by using byproduct of manganese steel alloy and silicon reducer | |
| CN115305313A (en) | Converter slag melting agent and preparation method and application thereof | |
| CN103936447A (en) | Ladle-mouth magnesia carbon brick added with pyrophyllite and preparation method of ladle-mouth magnesia carbon brick | |
| JP5910182B2 (en) | Hot metal manufacturing method using vertical melting furnace | |
| JP4462008B2 (en) | Method for producing sintered ore and pseudo particles for producing sintered ore containing reduced iron | |
| CN112593040B (en) | Converter vanadium extraction coolant and application thereof | |
| JP5251296B2 (en) | Hot metal production method using vertical melting furnace | |
| KR102688835B1 (en) | Operating method in the iron making process | |
| JP2010013683A (en) | Molten iron manufacturing method using vertical melting furnace | |
| JP2014040620A (en) | Boron additive |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20040812 |
|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20050812 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20070726 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20070807 |
|
| A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20071204 |