JP2009114515A - Method for operating blast furnace - Google Patents

Method for operating blast furnace Download PDF

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JP2009114515A
JP2009114515A JP2007290438A JP2007290438A JP2009114515A JP 2009114515 A JP2009114515 A JP 2009114515A JP 2007290438 A JP2007290438 A JP 2007290438A JP 2007290438 A JP2007290438 A JP 2007290438A JP 2009114515 A JP2009114515 A JP 2009114515A
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blast furnace
raw material
iron ore
sieve
surfactant
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Jun Ishii
純 石井
Takeshi Sato
健 佐藤
Yasuo Nagashima
康雄 長島
Koji Yamamoto
耕司 山本
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JFE Steel Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for operating a blast furnace, which can effectively utilize a conventional sieve facility as it is, improves the performance of removing deposited powders of raw materials for the blast furnace such as iron ore, at a comparatively low cost, and can reduce an amount of a fine powder to be brought into the blast furnace. <P>SOLUTION: The method for operating the blast furnace includes the steps of: preparing the raw material 1 in a wet condition for the blast furnace; adding a surface active agent 2 to the raw material and mixing them; and charging a material 6 remaining on a sieve after having been sieved into the blast furnace. It is preferable to use a fatty acid or an alkylbenzene sulfonic acid as the surface active agent, add the surface active agent 2 onto the raw material for the blast furnace on a belt conveyor 3 with a spray method, and mix the raw material 1 for the blast furnace with the surface active agent 2 by using an impact given in a connection fall 3a of the belt conveyor 3. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、製鉄プロセスにおいて、鉄鉱石等の高炉原料を篩い分けし、微粉を事前除去して高炉操業を効率的に行う手法に関する。   The present invention relates to a method for efficiently performing blast furnace operation by sieving blast furnace raw materials such as iron ore and removing fine powder in advance in an iron making process.

高炉を始めとする竪型炉による製鉄プロセスにおいては、充填層内に還元ガスを流通させて鉄鉱石を還元する必要があるため、効率的な操業を行う為には還元ガスが流通可能な空隙を確保する必要があり、鉄鉱石、コークス、焼結鉱等の装入原料は事前に微粉を除去しておく事が望ましい。このため各製鉄所においてはこれらの製鉄用原料から微粉を除去する篩い設備(振動篩い)を有している。しかしながらヤードで保管する原料等は、原料の保管の際、雨天等により水分含有率が高くなると微粉の付着力が高まるため、従来の篩いによる微粉除去は十分ではなかった。特に鉄鉱石は水分との親和性が高く、湿潤時の微粉の除去が非常に困難である。また、篩いのスクリーン上に粘土状の原料が付着して目詰まりを発生させる要因となっている。このため水分付着性の高い原料の篩い設備においては、通常目開きが大きい篩いが使用されてきた。たとえば、同じ高炉原料でも、焼結工場から直接送られる焼結鉱は殆ど水分を含まず微粉が落下しやすい為、微粉除去のために通常目開き4〜6mmの篩いが使用されているが、水分を含み微粉が付着している事が多い鉄鉱石の場合、粉の除去性能を高め、目詰まりを抑制するため通常目開き10mm程度の篩いが使用されている。つまり通常高炉原料としてそのまま使用できる4〜10mmの範囲の原料も篩い落とす事になり、歩留まりを大幅に低下させる要因となっている。また、目開き10mmの篩いを用いた場合でも、依然1mm以下の微粉の一部は10mm以上の鉱石に付着して落下せず、粉除去効率は大幅には向上していない。   In ironmaking processes using vertical furnaces such as blast furnaces, it is necessary to circulate reducing gas in the packed bed to reduce iron ore. It is desirable to remove fine powder in advance for the charging materials such as iron ore, coke, and sintered ore. For this reason, each steelworks has a sieving facility (vibrating sieving) for removing fine powder from these ironmaking raw materials. However, the raw material stored in the yard has not been sufficiently removed by conventional sieving since the adhesion of fine powder increases when the moisture content increases due to rain or the like during storage of the raw material. In particular, iron ore has a high affinity with moisture, and it is very difficult to remove fine powder when wet. In addition, the clay-like raw material adheres to the screen of the sieve and becomes a factor causing clogging. For this reason, in a raw material sieving equipment having a high moisture adhesion, a sieving having a large mesh has been used. For example, even in the same blast furnace raw material, since the sintered ore sent directly from the sintering plant contains almost no water and fine powder easily falls, a sieve with an opening of 4 to 6 mm is usually used for fine powder removal. In the case of iron ore, which contains water and often has fine powder adhered thereto, a sieve having an opening of about 10 mm is usually used in order to improve the removal performance of the powder and suppress clogging. That is, the raw material in the range of 4 to 10 mm that can be used as it is as a normal blast furnace raw material is also screened out, which is a factor for greatly reducing the yield. Further, even when a sieve having an opening of 10 mm is used, a part of fine powder of 1 mm or less still adheres to ore of 10 mm or more and does not fall, and the powder removal efficiency is not significantly improved.

鉄鉱石のような湿潤状態の原料の粉除去効率を向上させることのできる篩い分け手段としては、伸縮可能な篩網と、これを上下左右に連動させて変形しながら原料を運搬する可動機構を有する特殊スクリーン、例えばジャンピングスクリーン(登録商標)が知られている。ジャンピングスクリーン(登録商標)では、ウレタン製の網目に対して引っ張り・ゆるめの繰り返し運動を与える事により原料を跳ね上げ、落下の際の衝撃力で付着粉を分散させる効果が期待できる。また、網目が常に変形する為、湿潤原料を使用しても目詰まりが起こりにくいとされている。   As a sieving means that can improve the powder removal efficiency of wet raw materials such as iron ore, an expandable sieve mesh and a movable mechanism that conveys the raw material while deforming it in conjunction with up and down and left and right A special screen having, for example, a jumping screen (registered trademark) is known. With Jumping Screen (registered trademark), it is possible to expect the effect of dispersing the adhered powder by the impact force at the time of dropping, by applying the repetitive movement of pulling and loosening to the mesh made of urethane. Further, since the mesh is always deformed, clogging is unlikely to occur even when a wet raw material is used.

篩い分け以外の湿潤状態の原料の付着粉除去方法として、微粉が付着した鉄鉱石をスクリーン式ジェット洗浄機で水洗処理して付着粉を除去する方法が知られている(例えば、特許文献1参照。)。洗浄水をスクリーン上で勢い良く噴射するため鉄鉱石付着粉がきれいに洗浄され、付着粉を含んだ洗浄液はスクリーン式脱水機と液体サイクロンによって効率的に処理が可能であるとされている。
特許第3255775号
As a method for removing adhering powder of raw materials in a wet state other than sieving, a method is known in which iron ore to which fine powder has adhered is washed with a screen-type jet washer to remove the adhering powder (see, for example, Patent Document 1). .). It is said that the iron ore adhering powder is washed cleanly because the washing water is jetted on the screen vigorously, and the cleaning liquid containing the adhering powder can be efficiently processed by the screen-type dehydrator and the liquid cyclone.
Japanese Patent No. 3255775

上記のように、従来、湿潤時の付着粉が多い高炉原料は目開きの大きな篩い目を有する篩いで分級されてきたが、歩留が大幅に低下するものの依然篩い上に付着粉が混入し、付着粉除去効果は大きくなかった。   As mentioned above, blast furnace raw materials with a large amount of adhering powder when wet have been classified with a sieve having a large mesh opening, but the yield is greatly reduced, but the adhering powder is still mixed on the sieve. The adhering powder removal effect was not great.

また特殊スクリーンを用いた篩い分け法では、湿潤状態の原料の付着粉の分離性能は期待できるものの、スクリーン材質がウレタン等の樹脂材質で構成されており、さらに常に変形・伸縮するため、特に鉄鉱石などの硬質で比重の大きい材料を用いる場合、耐久性に問題がある。スクリーンの耐久性が低いと、スクリーン交換に伴うランニングコストが高額になるばかりでなく、交換のためにラインを止める頻度が高くなり、生産性悪化の大きな要因となる可能性が有る。また、従来製鉄所内で用いられている振動スクリーンとは形式が大きく異なるため、従来のスクリーンを撤去して新たに特殊スクリーンの設備を建設する必要があり、莫大な設備費用が必要になると予測される。従って、特殊スクリーンを用いた方法は製鉄原料用の篩い分け方法としてあまり普及していない。   In addition, the sieving method using a special screen can be expected to separate the adhering powder of the raw material in the wet state, but the screen material is made of a resin material such as urethane, and is constantly deformed and stretched. When using a hard material with a large specific gravity such as stone, there is a problem in durability. If the durability of the screen is low, not only the running cost associated with the screen replacement becomes high, but also the frequency of stopping the line for replacement becomes high, which may be a major factor in the deterioration of productivity. In addition, since the screen is very different from the vibrating screen used in the conventional steelworks, it is necessary to remove the conventional screen and construct a new special screen facility, which is expected to require enormous facility costs. The Therefore, the method using a special screen is not very popular as a sieving method for iron making raw materials.

さらに、スクリーン式ジェット洗浄機を用いて鉄鉱石を水洗処理する方法では、スクリーン式ジェット洗浄機、スクリーン式脱水機、液体サイクロン等の設備を新たに建設するために巨額の建設コストが必要となる。また特に鉄鉱石微粉を含んだ水処理に際しては、設備の磨耗が激しいためメンテナンスコストが高額になるという問題がある。さらに洗浄後の鉄鉱石に付着した水分による高炉への持ち込み水分が増加し、高炉炉頂温度を低下させ、操業を不安定化する要因となる可能性が有る。   Furthermore, in the method of washing iron ore with a screen jet washer, a huge construction cost is required to newly construct equipment such as a screen jet washer, a screen dehydrator, and a hydrocyclone. . Further, particularly in water treatment containing iron ore fine powder, there is a problem in that maintenance costs are high due to severe equipment wear. Furthermore, the moisture brought into the blast furnace due to the water adhering to the iron ore after washing may increase, lowering the blast furnace top temperature and destabilizing the operation.

そこで、本発明では、従来の篩い設備をそのまま有効活用することが可能であり、比較的安価に鉄鉱石等の高炉原料の付着粉除去性能を向上させ、高炉内に持ち込まれる微粉量を低減することのできる高炉の操業方法を提供することを目的とする。   Therefore, in the present invention, it is possible to effectively utilize the conventional sieving equipment as it is, and improve the performance of removing adhered powder from blast furnace raw materials such as iron ore at a relatively low cost, and reduce the amount of fine powder brought into the blast furnace. The purpose is to provide a method for operating a blast furnace.

本発明者らは、前記課題を解決するために、従来用いられている汎用の振動篩いを用いて、高炉原料の水分による付着粉を効率的に除去する手法について検討した。既存の篩い設備を用いて付着粉除去性能を改善する場合、高炉原料に与えることのできる振動エネルギーは一定であるため、水分による付着力自体を弱める必要があると考えられる。液体の架橋効果による粒子同士の付着力については、一般的に下記(a)式に示すような関係が知られている。   In order to solve the above-mentioned problems, the present inventors have studied a method for efficiently removing adhering powder due to moisture in a blast furnace raw material using a conventional general-purpose vibration sieve. When using the existing sieving equipment to improve the attached powder removal performance, the vibration energy that can be given to the blast furnace raw material is constant, so it is considered necessary to weaken the adhesive force itself due to moisture. Regarding the adhesion between particles due to the cross-linking effect of the liquid, a relationship as shown in the following formula (a) is generally known.

F=2πrσ/(1+tan(θ/2))・・・(a)
(F:付着力、σ:液体の表面張力、r:粒子半径、θ:液体架橋の粒子への接触角度)
上記(a)式によると、液体の架橋効果による付着力は、液体の表面張力に比例することが示されている。水はその分子構造が極性を有するため、分子同士がたがいに引き合い、大きな表面張力を持つ液体として知られている。水に界面活性剤を添加すると液体表面に界面活性剤分子が分散し、表面張力を大幅に低下させる事が可能である。
F = 2πrσ / (1 + tan (θ / 2)) (a)
(F: adhesion force, σ: surface tension of liquid, r: particle radius, θ: contact angle of liquid bridge to particle)
According to the above formula (a), it is shown that the adhesion due to the cross-linking effect of the liquid is proportional to the surface tension of the liquid. Since water has a polar molecular structure, water attracts each other and is known as a liquid having a large surface tension. When a surfactant is added to water, surfactant molecules are dispersed on the liquid surface, and the surface tension can be greatly reduced.

また界面活性剤の中でも特に脂肪酸塩類は、鉱石表面を親水性から疎水性に変化させる特性を有する。このため浮遊選鉱プロセスにおいては界面活性剤として添加し、鉱石表面が疎水性に変化したところにエアレーションを行い、浮上させて分離する手法が用いられている。鉱石表面が親水性から疎水性に変化すると、水分が付着しにくくなり、液体架橋自体が発生しにくくなる。   Among the surfactants, particularly fatty acid salts have the property of changing the ore surface from hydrophilic to hydrophobic. For this reason, in the flotation process, a method of adding as a surfactant and performing aeration on the surface of the ore where the ore surface has changed to hydrophobic to float and separate is used. When the ore surface is changed from hydrophilic to hydrophobic, it becomes difficult for moisture to adhere and liquid cross-linking itself hardly occurs.

上記の効果により、水分による付着効果が大幅に弱められるため、従来と同等の振動エネルギーを与えても大幅に付着粉の除去効果を高める事が可能となる。以上の知見から得られた本発明の特徴は以下の通りである。
(1)湿潤状態の高炉原料に界面活性剤を添加して混合し、篩い分けを行った篩い上を高炉に装入することを特徴とする高炉の操業方法。
(2)界面活性剤として、脂肪酸またはアルキルベンゼンスルホン酸を用いることを特徴とする、(1)に記載の高炉の操業方法。
(3)ベルトコンベア上の高炉原料上に界面活性剤を散布して添加し、前記ベルトコンベアの乗り継ぎ落差における衝撃を利用して前記高炉原料と前記界面活性剤とを混合することを特徴とする(1)または(2)に記載の高炉の操業方法。
Due to the above effect, the adhesion effect due to moisture is greatly weakened, so that it is possible to greatly enhance the effect of removing the adhered powder even when vibration energy equivalent to the conventional one is given. The characteristics of the present invention obtained from the above findings are as follows.
(1) A method of operating a blast furnace, comprising adding a surfactant to a wet blast furnace raw material, mixing the mixture, and charging the sieved sieve into the blast furnace.
(2) The method for operating a blast furnace according to (1), wherein fatty acid or alkylbenzenesulfonic acid is used as the surfactant.
(3) A surfactant is sprayed and added onto a blast furnace raw material on a belt conveyor, and the blast furnace raw material and the surfactant are mixed using an impact at a transfer drop of the belt conveyor. A method for operating a blast furnace according to (1) or (2).

本発明によれば、従来の篩い設備を用いながら、雨水等にさらされた鉄鉱石等の湿潤状態の高炉原料の篩い分けが容易に行えるようになる。これにより高炉に装入される微粉原料を十分に抑制する事が可能となり、高炉内の通気性が確保され操業安定性が向上する。また、高炉原料の表面が疎水化されることにより篩い下に落下する水分が増加するため、篩い上として高炉に持ち込まれる水分量が従来と比較して減少する。近年高炉操業においてはコークス使用量の削減により高炉炉頂温度が低下し水分が凝集してダスト排出が妨げられ易い状況にあるが、高炉装入原料の含有水分が減少すると原料の乾燥に必要な熱量が少なくなるため炉頂部において必要な温度(100℃以上)を確保しやすくなり、ダスト排出性能が向上し通気性を確保し易くなるという効果もある。   According to the present invention, while using a conventional sieving facility, sieving of wet blast furnace raw materials such as iron ore exposed to rainwater and the like can be easily performed. As a result, it is possible to sufficiently suppress the fine powder material charged into the blast furnace, ensuring air permeability in the blast furnace and improving operational stability. Moreover, since the surface of the blast furnace raw material is hydrophobized, the amount of moisture falling under the sieve increases, so the amount of moisture brought into the blast furnace as the sieve is reduced compared to the conventional case. In recent years in blast furnace operation, the temperature at the top of the blast furnace decreases due to the reduction of the amount of coke, and moisture is agglomerated and dust discharge tends to be hindered. Since the amount of heat is reduced, it is easy to secure a necessary temperature (100 ° C. or higher) at the top of the furnace, and there is an effect that dust discharge performance is improved and air permeability is easily secured.

本発明によれば、水分の存在により湿潤状態にある鉄鉱石等の高炉原料に界面活性剤を添加することで、微粉の付着力を弱めることができる為、高炉原料に界面活性剤を添加して混合し、篩い分けを行うことで、従来の篩い設備においても容易に微粉を除去することができる。そして、篩い分けにより微粉が除去された高炉原料である篩い上を、高炉に装入して操業を行ない、銑鉄を製造する。   According to the present invention, by adding a surfactant to a blast furnace raw material such as iron ore that is in a wet state due to the presence of moisture, the adhesion of fine powder can be weakened, so a surfactant is added to the blast furnace raw material. By mixing and sieving, the fine powder can be easily removed even in the conventional sieving equipment. Then, the top of the sieve, which is the raw material of the blast furnace from which fine powder has been removed by sieving, is charged into the blast furnace and operated to produce pig iron.

尚、湿潤状態とは、鉄鉱石等の粒子表面に水分が存在する状態である。鉄鉱石等の原料の含有水分量に対する界面活性剤の効果は、原料の粒子内部の気孔分布により異なるが(対象粒子内部の気孔に水分が吸収された後の粒子表面の水分が問題となるため)、原料の水分含有量が5mass%以上の場合に効果が大きい。   The wet state is a state in which moisture exists on the surface of particles such as iron ore. The effect of surfactants on the moisture content of raw materials such as iron ore varies depending on the pore distribution inside the raw material particles (because the moisture on the particle surface after the moisture is absorbed by the pores inside the target particles becomes a problem) ), The effect is large when the water content of the raw material is 5 mass% or more.

本発明は、高炉原料として鉄鉱石に用いる場合に最も効果的であるが、コークスや石炭、焼結鉱、石灰石等に用いる場合にも効果がある。   The present invention is most effective when used for iron ore as a blast furnace raw material, but is also effective when used for coke, coal, sintered ore, limestone, and the like.

本発明に用いる界面活性剤は、基本的にどのような種類のものも利用可能であるが、水中に容易に溶解・拡散するものが特に望ましい。水への溶解速度が遅い場合、溶解させる為に攪拌動力や時間を必要とするからである。また、鉱石等の高炉原料の表面に付着して親水性を疎水性に変換する効果をもつものがより望ましく、具体的には、ステアリン酸ナトリウムを始めとするオレイン酸、ラウリン酸、ステアリン酸のナトリウム塩、カリウム塩等の各種脂肪酸や、直鎖アルキルベンゼンスルホン酸ナトリウムなどを用いることが好ましい。これは、鉱石等の表面の水とのぬれ性を悪化させる事により、鉱石等と水との間の付着性を弱める効果が期待できる為である。   As the surfactant used in the present invention, basically any type of surfactant can be used, but those that dissolve and diffuse easily in water are particularly desirable. This is because when the dissolution rate in water is low, stirring power and time are required for dissolution. Further, those having the effect of converting hydrophilicity to hydrophobicity by adhering to the surface of blast furnace raw materials such as ores are more desirable. Specifically, oleic acid such as sodium stearate, lauric acid, stearic acid It is preferable to use various fatty acids such as sodium salt and potassium salt, sodium linear alkylbenzene sulfonate, and the like. This is because an effect of weakening the adhesion between the ore and the water can be expected by deteriorating the wettability of the surface of the ore and the like with water.

界面活性剤の添加方法としては、ヤード上で添加し重機で混合する方法、もしくはベルトコンベア上で鉱石等の高炉原料上に添加し、ベルトコンベアの乗り継ぎシュートにおける落下衝撃を利用して混合する方法などがあるが、混合効果が十分であれば後者の方法がより低コストであるため望ましい。また、ベルトコンベア上で界面活性剤を添加する位置は、篩いからなるべく離れていることが好ましく、原料ヤード側に近い位置とすることが望ましい。これは乗り継ぎ落差をより多く通過し、より多くの時間をかけて搬送されたほうが、界面活性剤が鉱石全体に行き渡りやすくなるためである。   As a method of adding a surfactant, a method of adding on a yard and mixing with a heavy machine, or a method of adding on a blast furnace raw material such as ore on a belt conveyor and mixing using a drop impact on a transfer chute of the belt conveyor However, if the mixing effect is sufficient, the latter method is desirable because it is less expensive. Further, the position where the surfactant is added on the belt conveyor is preferably as far as possible from the sieve, and is preferably close to the raw material yard side. This is because it becomes easier for the surfactant to reach the entire ore if it passes through the connecting drop more and is transported over a longer time.

図1は、本発明の一実施形態を示すフロー図である。微粉が付着した鉄鉱石1を高炉原料として用いる際に、界面活性剤2を、搬送ベルトコンベア3上の鉄鉱石1に上部から散布して添加する。界面活性剤2を添加された鉄鉱石1が、搬送ベルトコンベア3の乗り継ぎシュート部分3aで落下する際に、界面活性剤と鉄鉱石とが混合される。この状態で鉄鉱石1を、従来高炉装入前の鉄鉱石の篩い分けに用いている篩い設備4を用いて篩い分けを行うことで、鉄鉱石1は鉄鉱石微粉5と微粉除去後の鉄鉱石6とに分離され、篩い上の鉄鉱石6を高炉に装入することで、微粉の割合の少ない鉄鉱石を高炉に装入することが可能となる。   FIG. 1 is a flowchart showing an embodiment of the present invention. When using the iron ore 1 to which fine powder adheres as a blast furnace raw material, the surfactant 2 is added to the iron ore 1 on the conveyor belt conveyor 3 by spraying from above. When the iron ore 1 to which the surfactant 2 is added falls at the connecting chute portion 3a of the conveyor belt conveyor 3, the surfactant and the iron ore are mixed. In this state, the iron ore 1 is screened using the sieving equipment 4 used for screening the iron ore before charging the blast furnace, so that the iron ore 1 has the iron ore fine powder 5 and the iron ore after the fine powder is removed. By separating the iron ore 6 on the sieve into the blast furnace, it is possible to charge the iron ore with a small proportion of fine powder into the blast furnace.

本発明による効果を確認する為に、以下の条件で篩い分け試験を行った。   In order to confirm the effect of the present invention, a sieving test was conducted under the following conditions.

1、水分による粉付着性が高い鉄鉱石を用意し、幅2m、長さ3.5m、目開き7mmの振動篩いに約5Tを供して篩い分けを行った。鉄鉱石の水分含有量を乾燥法で測定したところ、3.9mass%であった。   1. Iron ore with high powder adhesion due to moisture was prepared, and sieved by applying about 5T to a vibrating sieve having a width of 2 m, a length of 3.5 m, and a mesh opening of 7 mm. It was 3.9 mass% when the moisture content of the iron ore was measured by the drying method.

2、上記1と同じ鉄鉱石に水分を散水した後、ショベルを用いてよく混合し、水分をなじませる為に数時間静置して湿潤状態とした。ここで再び鉄鉱石の水分含有量を乾燥法で測定したところ、9.3mass%となった。この湿潤鉄鉱石を前述の振動ふるいに約5T供し、篩い分けを行った。   2. After water was sprinkled on the same iron ore as in 1 above, it was mixed well using an excavator and allowed to stand for several hours in order to allow the water to blend into a wet state. Here, when the water content of the iron ore was measured again by the drying method, it was 9.3 mass%. The wet iron ore was subjected to about 5 T on the above-mentioned vibrating screen and sieved.

3、散水した上記2と同じ湿潤鉄鉱石に混合脂肪酸ナトリウムを鉄鉱石に対して0.5mass%添加し、ショベルを用いて良く攪拌した後、約5Tを上述の振動篩いに供して篩い分けを行った。添加した混合脂肪酸ナトリウムは、粒径1mm以下の乳白色の固形パウダー状であった。   3. Add 0.5 mass% of mixed fatty acid sodium to iron ore to the same wet iron ore as 2 above, sprinkle water, stir well with an excavator, then use about 5T for the above vibrating sieve and screen went. The added mixed fatty acid sodium was milky white solid powder having a particle size of 1 mm or less.

4、最後に、散水した上記2の湿潤鉄鉱石に直鎖アルキルベンゼンスルホン酸ナトリウム(LAS Na)を0.5mass%添加し、ショベルを用いて良く攪拌した後、約5Tを上述の振動篩いに供して篩い分けを行った。添加した添加した直鎖アルキルベンゼンスルホン酸ナトリウムは、粒径1mm以下の白色の固形パウダー状であった。   4. Finally, 0.5 mass% of linear alkylbenzene sulfonate (LAS Na) is added to the wet iron ore of 2 above, and after stirring well with an excavator, about 5T is applied to the above vibration sieve. And sieved. The added sodium alkylbenzene sulfonate was in the form of a white solid powder having a particle size of 1 mm or less.

以上の1〜4の篩い分け後の「篩い下質量比率」と、「篩い下粒径5mm以下(−5mm)回収率」の測定結果を表1に示す。   Table 1 shows the measurement results of “mass ratio under sieving” after sieving 1 to 4 above and “recovery rate under particle size of 5 mm or less (−5 mm)”.

Figure 2009114515
Figure 2009114515

鉄鉱石に水分を添加した湿潤鉄鉱石を篩い分けすると、篩い下質量比率(篩い下質量÷篩い供給質量×100)が大幅に低下した。そこで、篩い下−5mm回収率(篩い下−5mm質量÷篩い供給−5mm質量×100)を計算すると、同様に回収率が大幅に低下しており、−5mm粉が大量に篩い上試料に付着している事が確認された。混合脂肪酸ナトリウムを添加混合した条件においては、湿潤鉄鉱石のみの場合と比較して篩い下重量比率が大幅に増加した。篩い下−5mm回収率も水分添加前に近いレベルまで回復しており、界面活性剤により付着粉が篩い落とされる効果が確認さされた。また、直鎖アルキルベンゼンスルホン酸ナトリウムを添加混合した条件においても同様の結果が示され、付着粉除去効果が示された。   When the wet iron ore obtained by adding moisture to the iron ore is sieved, the mass ratio under sieve (mass under sieve ÷ mass of sieve feed × 100) is greatly reduced. Therefore, when the sieving -5 mm recovery rate (under sieving -5 mm mass ÷ sieving supply -5 mm mass x 100) is calculated, the recovery rate is also greatly reduced, and a large amount of -5 mm powder adheres to the sieving sample. It was confirmed that Under the condition where the mixed fatty acid sodium was added and mixed, the weight ratio under the sieve was greatly increased as compared with the case of only the wet iron ore. The sieving -5 mm recovery was also restored to a level close to that before the addition of water, and the effect of sieving the adhered powder by the surfactant was confirmed. Moreover, the same result was shown also in the conditions which added and mixed sodium linear alkylbenzenesulfonate, and the adhering powder removal effect was shown.

本発明の一実施形態を示すフロー図。The flowchart which shows one Embodiment of this invention.

符号の説明Explanation of symbols

1 鉄鉱石
2 界面活性剤
3 搬送ベルトコンベア
3a 乗り継ぎシュート部分
4 篩い設備
5 鉄鉱石微粉
6 微粉除去後の鉄鉱石
DESCRIPTION OF SYMBOLS 1 Iron ore 2 Surfactant 3 Conveyor belt conveyor 3a Transfer chute part 4 Sieve equipment 5 Iron ore fine powder 6 Iron ore after fine powder removal

Claims (3)

湿潤状態の高炉原料に界面活性剤を添加して混合し、篩い分けを行った篩い上を高炉に装入することを特徴とする高炉の操業方法。   A method of operating a blast furnace, comprising adding a surfactant to a wet blast furnace raw material, mixing the mixture, and charging the sieved sieve into the blast furnace. 界面活性剤として、脂肪酸またはアルキルベンゼンスルホン酸を用いることを特徴とする、請求項1に記載の高炉の操業方法。   The method for operating a blast furnace according to claim 1, wherein fatty acid or alkylbenzene sulfonic acid is used as the surfactant. ベルトコンベア上の高炉原料上に界面活性剤を散布して添加し、前記ベルトコンベアの乗り継ぎ落差における衝撃を利用して前記高炉原料と前記界面活性剤とを混合することを特徴とする請求項1または請求項2に記載の高炉の操業方法。   2. A surfactant is sprayed and added onto a blast furnace raw material on a belt conveyor, and the blast furnace raw material and the surfactant are mixed using an impact at a transfer drop of the belt conveyor. Or the operating method of the blast furnace of Claim 2.
JP2007290438A 2007-11-08 2007-11-08 Method for operating blast furnace Pending JP2009114515A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012132062A (en) * 2010-12-21 2012-07-12 Jfe Steel Corp Sieving method of metallurgical coke and sieving facility of metallurgical coke

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012132062A (en) * 2010-12-21 2012-07-12 Jfe Steel Corp Sieving method of metallurgical coke and sieving facility of metallurgical coke

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