JPH0135885B2 - - Google Patents
Info
- Publication number
- JPH0135885B2 JPH0135885B2 JP919783A JP919783A JPH0135885B2 JP H0135885 B2 JPH0135885 B2 JP H0135885B2 JP 919783 A JP919783 A JP 919783A JP 919783 A JP919783 A JP 919783A JP H0135885 B2 JPH0135885 B2 JP H0135885B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- pig iron
- steel
- parts
- less
- 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
- 239000003795 chemical substances by application Substances 0.000 claims description 16
- 229910000831 Steel Inorganic materials 0.000 claims description 15
- 239000010959 steel Substances 0.000 claims description 15
- 229910000805 Pig iron Inorganic materials 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 12
- 229910000278 bentonite Inorganic materials 0.000 claims description 11
- 239000000440 bentonite Substances 0.000 claims description 11
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims description 11
- 239000002893 slag Substances 0.000 claims description 11
- 238000000465 moulding Methods 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 238000009628 steelmaking Methods 0.000 claims description 7
- 239000011230 binding agent Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 4
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 4
- 239000000428 dust Substances 0.000 claims description 4
- 239000004571 lime Substances 0.000 claims description 4
- 238000005255 carburizing Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 230000005484 gravity Effects 0.000 description 4
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 3
- 239000004372 Polyvinyl alcohol Substances 0.000 description 3
- 238000005054 agglomeration Methods 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000001768 carboxy methyl cellulose Substances 0.000 description 3
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 3
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 3
- 239000003610 charcoal Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 229920002451 polyvinyl alcohol Polymers 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 229910017082 Fe-Si Inorganic materials 0.000 description 2
- 229910017133 Fe—Si Inorganic materials 0.000 description 2
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 2
- 244000046052 Phaseolus vulgaris Species 0.000 description 2
- -1 charcoal Chemical compound 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
- C21C1/025—Agents used for dephosphorising or desulfurising
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Description
本発明は製鋼用加炭剤の製造方法に関するもの
である。
現在各種の加炭剤が用いられているが、あるも
のは比重が小さ過ぎて溶解中に浮上し十分に混合
されない、又あるものは用いる結合剤が高価過ぎ
て実用性に乏しい等一長一短があつた。即ち豆炭
等殆んどが炭素分のものは比重が小さ過ぎるし、
結合剤として有機物たるPVA(ポリビニルアルコ
ール)やCMC(カルボキシメチルセルロース)は
結合力が大なので極く少量(約1%位)でよいが
この様な少量を全体均一に混合するのは困難であ
り、かつこのPVAやCMCは非常に高価であるの
で製鋼用加炭剤の如く大量に使用するものに対し
ては実用上不向きなのである。
本発明は上述の諸問題を解消する加炭剤の製造
方法を提供せんとするものであり、その要旨は、
製銑、製鋼工程で発生する各種スラグあるいはダ
ストから得た粒径3mm以下の粒銑あるいは粒鋼30
〜70重量%と残部が粒径3mm以下の炭素粉粒物と
の混合物100重量部に対し、結合剤としてベント
ナイトを3〜8重量部添加し、かつ水を成型時の
水分含有率が5〜10重量%となる如く添加し、混
合後塊状物に成型することを特徴とする加炭剤の
製造方法であり、用いる結合剤としてのベントナ
イトはその1/2以下をCaOで置換することもあり
得る。
なおここで用いる粒銑というのは高炉スラグ、
溶銑の脱硫や脱隣等の炉外精練工程で生ずるスラ
グから選別した粒銑の事を指称し、これらのスラ
グから得られる鉄銑は通常炭素を3〜4重量%含
有している為に、それを上述の如く加炭剤の成分
として用いた場合溶湯中での溶解が速やかに進行
するという特長がある。又粒鋼というのは転炉や
電気炉の製鋼炉スラグ又は転炉ダストから選別し
た粒鋼の事を指称し、これらの粒鋼は本発明によ
る加炭剤を製鋼工程の末期で用いる場合に好都合
である、即ち製鋼工程の末期ではPやSの高い銑
鉄を用いるよりはPやSが低くしかも既に鋼とな
つている粒鋼を用いた方がよいからである。
以下本発明を開発するに至つた一連の試験及び
その結果について述べる。
まず用いた各種原材料の代表的な組成は下記第
1表、第2表の通りである。
The present invention relates to a method for producing a recarburizing agent for steel manufacturing. Various types of carburizing agents are currently used, but some have advantages and disadvantages, such as some having too low a specific gravity and floating during melting and not being sufficiently mixed, and others using binders that are too expensive to be practical. Ta. In other words, the specific gravity of beans that are mostly carbon, such as charcoal, is too low.
PVA (polyvinyl alcohol) and CMC (carboxymethylcellulose), which are organic substances, can be used as binding agents in very small amounts (approximately 1%) because they have a large binding force, but it is difficult to mix such small amounts uniformly throughout the product. Moreover, since PVA and CMC are very expensive, they are not practically suitable for applications where they are used in large quantities, such as recarburizing agents for steelmaking. The present invention aims to provide a method for producing a recarburizing agent that solves the above-mentioned problems, and the gist thereof is as follows:
Granular pig iron or granular steel with a grain size of 3 mm or less obtained from various slags or dust generated in the pig iron making and steel making processes30
3 to 8 parts by weight of bentonite as a binder is added to 100 parts by weight of a mixture of ~70% by weight and the balance is carbon powder with a particle size of 3 mm or less, and the water content at the time of molding is 5 to 100 parts by weight. This is a method for producing a carburizing agent characterized by adding 10% by weight of bentonite and forming it into a lump after mixing. Less than half of the bentonite used as a binder may be replaced with CaO. obtain. The granular pig iron used here is blast furnace slag,
It refers to granular pig iron that is selected from slag produced in outside-furnace smelting processes such as hot metal desulfurization and desulfurization, and iron pig iron obtained from these slags usually contains 3 to 4% carbon by weight. When it is used as a component of a recarburizing agent as described above, it has the advantage that dissolution in the molten metal progresses rapidly. In addition, granular steel refers to granular steel selected from steelmaking furnace slag or converter dust of a converter or electric furnace, and these granular steels can be used when the recarburizer according to the present invention is used at the final stage of the steelmaking process. This is because it is convenient, that is, at the final stage of the steelmaking process, it is better to use granular steel, which has low P and S content and has already become steel, rather than using pig iron with high P and S content. The series of tests that led to the development of the present invention and their results will be described below. First, typical compositions of the various raw materials used are shown in Tables 1 and 2 below.
【表】【table】
【表】
この様な原材料を下記第3表に示す割合に配合
して試料No.1、2、3の3種類を造つた。[Table] Three types of samples, Nos. 1, 2, and 3, were prepared by blending these raw materials in the proportions shown in Table 3 below.
【表】
なお第3表中の単位は、粒銑、粒鋼、粉コーク
ス及びFe−Siについてはそれら全体を100重量%
とした場合の重量%で、ベントナイト及び石灰に
ついては粒銑、粒鋼、粉コークス及びFe−Siの
合計を100重量部とした場合の重量部である。
この第3表に示す様な試料に対しそれぞれ水を
6〜9重量%加えて混合後、製団機で塊状物とな
し製品たる加炭剤を得た。得られた加炭剤の諸特
性を下記第4表に示す。なお第4表中製品No.はそ
れぞれ同No.の上記試料から得られた製品加炭剤を
示す(以下同じ)。[Table] The units in Table 3 are 100% by weight for granular pig iron, granular steel, coke powder, and Fe-Si.
Bentonite and lime are parts by weight when the total of granular pig iron, granular steel, coke powder, and Fe-Si is 100 parts by weight. 6 to 9% by weight of water was added to each of the samples as shown in Table 3, and after mixing, a lump material was formed using a compactor to obtain a recarburizing agent as a product. The properties of the obtained recarburizer are shown in Table 4 below. Note that the product numbers in Table 4 indicate the product recarburizing agents obtained from the above samples with the same numbers (the same applies hereinafter).
【表】
本発明方法により得られる加炭剤は、その混合
や製団(塊状化)中に、主として鉄の酸化反応に
起因する発熱反応があり、製団直後ではその温度
が90〜100℃となり、この熱で製品加炭剤が自ら
養生される形態となる利点があるが、その度合を
示す製品加炭剤中の水分の経時変化を下記第5表
に示す。[Table] The carburizing agent obtained by the method of the present invention undergoes an exothermic reaction mainly due to the oxidation reaction of iron during its mixing and agglomeration (agglomeration), and the temperature immediately after the agglomeration is 90 to 100℃. Therefore, there is an advantage that the product carburizing agent is cured by itself with this heat, and Table 5 below shows the change in water content in the product carburizing agent over time showing the degree of curing.
【表】
次に上述の方法で得た試料No.1と比較試料とし
て炭素分87重量%の豆炭とにつき、その双方とも
溶鋼鍋内の底部にそれらを敷置し、その上から溶
鋼を注湯するという方法で加炭効果を比較した結
果、比較試料である豆炭の炭素分の歩留が51%で
あつたのに比べ、本は発明試料No.1のそれは57%
と大きく向上していた。なお加炭剤の用い方は上
述の如く敷置して用いる方式の他、溶湯中に押込
む等各種の方式があり、その方式によつて炭素分
の歩留に大きな差異が出るが、上述の如く単に敷
置して何ら撹拌する事なく用いる方式では一般に
その歩留は低く本発明試料No.1の57%というのは
歩留が高い方である事を言い添えておく。
ところで本発明で用いる粒銑、粒鋼及びコーク
ス等の炭素粉はその粒度が3mmより大であると、
まず成型時に成型圧が加わり難く十分な強度のも
のが得られない事、更には製品を加炭剤として用
いた場合に溶融し難い等の欠点がある。
又粒銑、粒鋼の配合割合を30〜70重量%とした
のは、これらが30重量%より少ないと得られる加
炭剤の比重が小さく溶滓上に浮上するか若しくは
溶滓中に停留して加炭効果が小さくなるし、70重
量%を越えると炭素分が不足し同じく加炭効果が
小さくなるからである。
ベントナイトの量は、3重量部よりも少ないと
全体が十分に粒調性を有さず、逆に多くなり過ぎ
8重量部を過ぎると成型時に成型圧がかかり難く
なるので3〜8重量部とする。
次に水分の量も成型時に十分圧力がかかるとい
う点から考えて5〜10重量%とする。
又石灰をベントナイトと併用するのは、ベント
ナイト中にはCaO分が少ないので、成分調整をも
兼ねそれ自体としても相当の結合性を有する石灰
を用いるが、結合性の点でその量はベントナイト
の1/2以下とする。
以上述べて来た如く、本発明方法によれば上記
各種原材料は全て通常は埋立て等にしか用いられ
ていない各種スラグあるいはダスト、又は広く日
本全土に存在するベントナイト等を活用する事に
より、かつ特別な養生設備、養生場所を設ける事
なく自らの酸化発熱反応により自己養生を起こし
強固に固まり、そして得られた加炭剤はその中に
鉄分を多く含むので取扱いが磁着力を応用した吊
下運搬機を用いる事が出来、それを実際に加炭剤
として用いた場合第4表から明らかな如く溶滓と
比較して比重が大であり溶湯面まで速やかに到達
する為溶湯とよく反応し高い加炭効果を示すもの
である。[Table] Next, sample No. 1 obtained by the above method and miniature charcoal with a carbon content of 87% by weight as a comparison sample were placed on the bottom of a molten steel ladle, and molten steel was poured over them. As a result of comparing the carburization effect by boiling in hot water, the carbon content yield of the comparison sample, bean charcoal, was 51%, while that of invention sample No. 1 was 57%.
It was a big improvement. There are various ways to use the carburizing agent, such as placing it on the ground as described above, and pushing it into the molten metal. Depending on the method, there is a large difference in the carbon content yield, but the method described above It should be added that the method of simply placing the sample and using it without any stirring generally has a low yield, and the 57% yield of sample No. 1 of the present invention is on the high side. By the way, when the particle size of the carbon powder such as granular pig iron, granular steel, and coke used in the present invention is larger than 3 mm,
First, it is difficult to apply molding pressure during molding, making it difficult to obtain a product with sufficient strength.Additionally, the product has drawbacks such as difficulty in melting when used as a carburizing agent. The reason why the blending ratio of granular pig iron and granular steel is set to 30 to 70% by weight is because if these are less than 30% by weight, the specific gravity of the recarburizer obtained will be small and will float on the slag or remain in the slag. If it exceeds 70% by weight, the carbon content will be insufficient and the carburizing effect will also be reduced. If the amount of bentonite is less than 3 parts by weight, the grain quality will not be sufficient as a whole, and if it is too large, and if it exceeds 8 parts by weight, it will be difficult to apply molding pressure during molding, so it should be 3 to 8 parts by weight. do. Next, the amount of water is set at 5 to 10% by weight in order to ensure that sufficient pressure is applied during molding. In addition, lime is used in combination with bentonite because bentonite has a low CaO content, so lime is used to adjust the composition and has considerable binding properties by itself. It should be 1/2 or less. As described above, according to the method of the present invention, all of the above-mentioned various raw materials are made by utilizing various slags or dusts that are normally used only in landfills, or bentonite, which exists widely throughout Japan, and It self-cures through its own oxidative exothermic reaction without the need for special curing equipment or a curing place, and hardens solidly.The resulting recarburizer contains a large amount of iron, so it must be handled by hanging using magnetic force. A transporter can be used, and when it is actually used as a carburizing agent, as is clear from Table 4, it reacts well with the molten metal because it has a higher specific gravity than molten slag and quickly reaches the molten metal surface. It shows a high carburizing effect.
Claims (1)
はダストから得た粒径3mm以下の粒銑あるいは粒
鋼30〜70重量%と残部が粒径3mm以下の炭素粉粒
物との混合物100重量部に対し、結合剤としてベ
ントナイトを3〜8重量部添加し、かつ水を成型
時の水分含有率が5〜10重量%となる如く添加
し、混合後塊状物に成型することを特徴とする加
炭剤の製造方法。 2 製銑、製鋼工程で発生する各種スラグあるい
はダストから得た粒径3mm以下の粒銑あるいは粒
鋼30〜70重量%と残部が粒径3mm以下の炭素粉粒
物との混合物100重量部に対し、結合剤としてベ
ントナイトと同ベントナイトの1/2以下の石灰と
を合計で3〜8重量部添加し、かつ水を成型時の
水分含有率が5〜10重量%となる如く添加し、混
合後塊状物に成型することを特徴とする加炭剤の
製造方法。[Scope of Claims] 1. 30 to 70% by weight of granular pig iron or granular steel with a particle size of 3 mm or less obtained from various slags or dust generated in pig iron making and steel making processes, and the balance being carbon powder particles with a particle size of 3 mm or less. To 100 parts by weight of the mixture, add 3 to 8 parts by weight of bentonite as a binder, and add water such that the water content at the time of molding is 5 to 10% by weight, and after mixing, mold into a lump. A method for producing a recarburizing agent characterized by: 2 100 parts by weight of a mixture of 30 to 70% by weight of granulated pig iron or granulated steel with a particle size of 3 mm or less obtained from various slags or dust generated in the pig iron making and steel making processes, and the balance of carbon powder particles with a particle size of 3 mm or less. On the other hand, a total of 3 to 8 parts by weight of bentonite and lime, which is less than 1/2 of the bentonite, is added as a binder, and water is added so that the moisture content at the time of molding is 5 to 10% by weight, and mixed. A method for producing a recarburizing agent, which is characterized in that it is then molded into a lump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP919783A JPS59136410A (en) | 1983-01-21 | 1983-01-21 | Manufacture of carburizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP919783A JPS59136410A (en) | 1983-01-21 | 1983-01-21 | Manufacture of carburizer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59136410A JPS59136410A (en) | 1984-08-06 |
| JPH0135885B2 true JPH0135885B2 (en) | 1989-07-27 |
Family
ID=11713777
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP919783A Granted JPS59136410A (en) | 1983-01-21 | 1983-01-21 | Manufacture of carburizer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59136410A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19654501C1 (en) * | 1996-12-18 | 1998-08-20 | Mannesmann Ag | Processes for hot metal desulfurization |
| JP6622755B2 (en) * | 2017-06-09 | 2019-12-18 | 株式会社サンアール | Carburizing agent for steel making and steel making method |
| CN109722498B (en) * | 2019-02-28 | 2020-06-30 | 河南师范大学新联学院 | Desulfurizing agent for waste phosphorus pig iron and desulfurization and recarburization method thereof |
-
1983
- 1983-01-21 JP JP919783A patent/JPS59136410A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59136410A (en) | 1984-08-06 |
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