JPH0834643A - Steelmaking slag pulverization inhibitor and method for producing the same - Google Patents
Steelmaking slag pulverization inhibitor and method for producing the sameInfo
- Publication number
- JPH0834643A JPH0834643A JP6193790A JP19379094A JPH0834643A JP H0834643 A JPH0834643 A JP H0834643A JP 6193790 A JP6193790 A JP 6193790A JP 19379094 A JP19379094 A JP 19379094A JP H0834643 A JPH0834643 A JP H0834643A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- weight
- steelmaking slag
- agent
- glass
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Manufacture Of Iron (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、製鋼スラグの冷却過程
において自己崩壊,粉化を起こす現象を防止するための
スラグ粉化防止剤及びその製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a slag dusting preventive agent for preventing the phenomenon of self-disintegration and pulverization in the cooling process of steelmaking slag, and a method for producing the same.
【0002】[0002]
【従来の技術】製鋼スラグ、とりわけステンレス製鋼ス
ラグに関し、塩基度(CaO/SiO 2重量比)約1.
5以上のスラグは、その冷却過程において2CaO・S
iO2の相転移によりα型相よりα′型へ、更にγ型又
はβ型へと転移する性質があり、多くの場合α′型より
γ型へ転移する際、約14%の体積膨張を伴なうために
スラグ自体が自己崩壊し粉化することが知られている。2. Description of the Related Art Steelmaking slag, especially stainless steelmaking slag
Regarding lag, basicity (CaO / SiO 2Weight ratio) About 1.
Slag of 5 or more is 2CaO · S during the cooling process.
iO2Phase transition from α-type to α′-type, γ-type or
Has the property of transferring to β type, and in many cases
In order to accompany the volume expansion of about 14% when transferring to γ type
It is known that the slag itself self-disintegrates and powders.
【0003】この粉化現象が作業環境を悪化させ、さら
にスラグ中のメタル回収時の回収後残渣としての脱水ケ
ーキが大量に発生する等の問題が、スラグ処理に対する
製鋼メーカーの負担増大の大きな原因になっている。This pulverization phenomenon deteriorates the working environment, and further, a large amount of dehydrated cake as a residue after recovery when recovering metal in slag is a major cause of increasing the burden on steelmakers for slag treatment. It has become.
【0004】このスラグの粉化を防止し固化させること
は、排出スラグを道路等の土木用骨材として有効に二次
利用できることもあって、製鋼メーカーの積年にわたる
課題となっている。[0004] Preventing the slag from pulverizing and solidifying it has been a long-standing problem for steel manufacturers because the discharged slag can be effectively used as a secondary aggregate for civil engineering such as roads.
【0005】スラグ粉化を抑制する方法としては、次の
方法が挙げられる。The following methods may be mentioned as methods for suppressing slag pulverization.
【0006】(1)スラグ出滓時に水砕ガラス化する方
法。(1) A method in which granulated glass is formed when slag is discharged.
【0007】(2)2CaO・SiO2スラグにSiO2
源を加えCaO・SiO2を主体とした塩基度1.5以
下(実質的にはスラグ組成によって多少変動する)のス
ラグに改質する方法。[0007] (2) SiO 2 in 2CaO · SiO 2 slag
A method in which a source is added and the slag is composed mainly of CaO.SiO 2 and has a basicity of 1.5 or less (substantially varies slightly depending on the slag composition).
【0008】(3)密度変化の大きいα′型からγ型へ
の相転移を抑制し、密度変化の小さいα′型からβ型へ
の相転移を促進させる方法。(3) A method of suppressing the α′-type to γ-type phase transition having a large density change and promoting the α′-type to β-type phase transition having a small density change.
【0009】このうち、(1)の方法では、スラグ出滓
時に随伴される溶融メタルにより水砕時に水蒸気爆発を
発生する恐れのある点、水砕物では軟質により土木用骨
材用途としての十分な強度を有し得ない点があるけれど
も、一部では実用化されている。Of these, the method (1) may cause a steam explosion during water granulation due to the molten metal that accompanies the slag slag, and the granulated material is soft enough for use as an aggregate for civil engineering. Although it cannot have strength, it has been put to practical use in some areas.
【0010】(2)の方法は、現在SiO2系改質剤と
して市販されているものもあるが、溶融スラグに対し、
約20%もの大量のSiO2を必要とするため、投入設
備,攪拌設備設置の必要があり、更に添加に伴なう溶滓
の温度低下によるスラグの増粘を生じ、作業性およびコ
スト面で不適当である。In the method (2), there is a commercially available SiO 2 type modifier at present, but for the molten slag,
Since a large amount of SiO 2 of about 20% is required, it is necessary to install charging equipment and stirring equipment, and further increase the viscosity of the slag due to the temperature decrease of the molten slag accompanying addition, and in terms of workability and cost. Inappropriate.
【0011】(3)の方法、すなわちα′型からβ型へ
の相転移については、かなり古くから研究が行なわれて
おり、種々の方法が提案されている。これらの方法のう
ち、スラグ中Si+4イオンよりイオン半径の小さいB+3
でSi+4を置換する方法が、有効な方法として提案され
ている(特開昭53−43690号公報、川鉄技報Vo
l.18,No.1(1986)20−24)。The method (3), that is, the phase transition from α'type to β type has been studied for a long time and various methods have been proposed. Among these methods, B +3 having an ion radius smaller than that of Si +4 ion in slag
The method of substituting Si +4 by means of the method has been proposed as an effective method (Japanese Patent Laid-Open No. 53-43690, Kawatetsu Technical Report Vo.
l. 18, No. 1 (1986) 20-24).
【0012】しかしながら、かかる従来のホウ素系のス
ラグ粉化防止剤は微粉末状で、かつそれ自体が含水物で
あるため、溶融スラグと接触する際に脱水気化反応とあ
いまって、スラグ粉化防止剤の吹き上げ現象を生じ、作
業環境を著しく悪化させると共に、ときには危険を伴う
のでその操作が非常に難かしい。更に、スラグ粉化防止
剤自体の溶融温度は低いものの粘性が高いためにスラグ
顕熱だけではスラグ中への拡散,混合が不十分で、スラ
グ粉化防止効果が発現し難いという問題がある。However, since the conventional boron-based slag dusting preventive agent is in the form of fine powder and is itself a water-containing substance, it is combined with a dehydration vaporization reaction when it comes into contact with molten slag to prevent slag dusting. The agent is blown up, the working environment is significantly deteriorated, and sometimes dangerous, so that its operation is very difficult. Furthermore, since the melting temperature of the slag dusting inhibitor itself is low, but its viscosity is high, there is a problem that the slag dusting prevention effect is difficult to be manifested because the diffusion and mixing into the slag are insufficient only by the slag sensible heat.
【0013】また、従来のホウ素系のスラグ粉化防止剤
はスラグとの化学組成が大幅に異なるために、溶融スラ
グに対し、粘度,密度に差が生じ易く、いわゆるスラグ
とスラグ粉化防止剤との親和性が悪く拡散混合能力が小
さいという欠点がある。Further, since the conventional boron-based slag dusting agent has a chemical composition greatly different from that of slag, a difference in viscosity and density is likely to occur with respect to the molten slag, so-called slag and slag dusting inhibitor. It has a disadvantage that it has a poor affinity with and has a small diffusive mixing ability.
【0014】ホウ素系のスラグ粉化防止剤の従来の欠点
を解消するためには、次の事項を考慮する必要がある。In order to solve the conventional drawbacks of the boron-based slag dusting preventive agent, the following matters should be taken into consideration.
【0015】溶滓への添加に伴ない、発塵,有害ガス
発生等による作業環境悪化を起こさず、かつ操作上安全
であること。The work environment is not deteriorated due to dust generation, harmful gas generation, etc. accompanying addition to the molten slag, and it is safe in operation.
【0016】溶滓への添加によりスラグ温度の大幅な
低下、増粘を生じないよう添加量が少なくて済むこと。The addition amount to the slag should be small so that the slag temperature is not significantly lowered and the viscosity is not increased.
【0017】溶融スラグとの粘度,密度差が小さく、
いわゆる親和力の高い化学組成を有するものであるこ
と。The viscosity and density difference from the molten slag are small,
It must have a so-called high affinity chemical composition.
【0018】本出願人は、上記の欠点を解消し得る製鋼
スラグの粉化防止剤として、ホウ珪酸アルカリガラスの
砂状粉体を有効成分とする粉化防止剤を提案した(特公
平5−50456号公報)。この粉化防止剤は、従来の
結晶性ホウ酸塩化合物の微粉末とは異なり、無水の砂状
粉体であるため、作業性に優れ、安全性良く粉化防止を
行うことができ、広く実用に供されている。The present applicant has proposed an anti-dusting agent containing a sandy powder of alkali borosilicate glass as an active ingredient, as an anti-dusting agent for steelmaking slag which can solve the above-mentioned drawbacks (Japanese Patent Publication No. 50456 publication). Unlike the conventional fine powder of a crystalline borate compound, this powdering inhibitor is an anhydrous sandy powder, so it has excellent workability and can perform powdering prevention with good safety, and is widely used. It is put to practical use.
【0019】[0019]
【発明が解決しようとする課題】本発明の目的は、上記
本出願人によるスラグ粉化防止剤を基礎にし、溶融スラ
グに対する溶融性が良く、また、より低コストで製造で
きる製鋼スラグの粉化防止剤及びその製造方法を提供す
ることにある。The object of the present invention is to pulverize the steelmaking slag, which is based on the above-mentioned slag dusting preventive agent of the present applicant, has good meltability with respect to molten slag, and can be produced at a lower cost. An object is to provide an inhibitor and a method for producing the same.
【0020】[0020]
【課題を解決するための手段及び作用】本発明者は、ホ
ウ珪酸アルカリガラスの利点を活かしつつ、更に改良す
べく研究を重ねたところ、フレーク状ガラスが極めて溶
融スラグとの親和性が高く、粉化防止剤として優れ、且
つ、工業的に有利に製造できることを知見し、本発明を
完成した。Means and Actions for Solving the Problems The present inventor, while taking advantage of the advantages of alkali borosilicate glass, further researched for further improvement, and found that the glass flakes had a very high affinity with molten slag, The present invention has been completed by finding that it is excellent as a dusting inhibitor and can be industrially advantageously produced.
【0021】すなわち、本発明は、フレーク状のホウ珪
酸アルカリガラスを有効成分とする製鋼スラグの粉化防
止剤に関する。That is, the present invention relates to a powdering inhibitor for steelmaking slag containing flake-shaped alkali borosilicate glass as an active ingredient.
【0022】また、本発明は、ガラス組成としてB
2O3:20〜50重量%、MO:10〜40重量%(但
し、MはCa,Mgを表す。)、SiO2:10〜35
重量%およびNa2O:5〜20重量%となるようにホ
ウ素、カルシウム(及び/又はマグネシウム)、珪素お
よびナトリウムの1種又は2種以上含有する原料を調合
し、次いで得られる調合物を加熱溶融した後、該融液を
フレイカーに流下し、次いで固化および粒度調整して、
フレーク状のホウ珪酸アルカリガラスを有効成分とする
製鋼スラグの粉化防止剤を製造する方法に関する。In the present invention, the glass composition is B
2 O 3 : 20 to 50% by weight, MO: 10 to 40% by weight (however, M represents Ca and Mg), SiO 2 : 10 to 35.
% By weight and Na 2 O: 5 to 20% by weight, a raw material containing one or more of boron, calcium (and / or magnesium), silicon and sodium is prepared, and then the obtained composition is heated. After melting, the melt is cast down into a flaker, then solidified and particle size adjusted,
The present invention relates to a method for producing an anti-dusting agent for steelmaking slag containing flake-shaped alkali borosilicate glass as an active ingredient.
【0023】以下、本発明について説明する。The present invention will be described below.
【0024】本発明にかかるホウ素系の製鋼スラグの粉
化防止剤(以下「スラグ粉化防止剤」という)は、従来
の結晶性ホウ酸塩化合物の微粉末とは異なり、ホウ珪酸
アルカリガラスのフレーク状粉体であることを特徴とす
る。The boron-based steelmaking slag dusting preventive agent (hereinafter referred to as "slag dusting inhibitor") according to the present invention is different from the conventional fine powder of crystalline borate compound in the alkali borosilicate glass. It is characterized in that it is a flake powder.
【0025】このガラスは製鋼スラグ(以下単に「スラ
グ」という)の溶融物との親和性は結晶性ホウ酸塩化合
物よりも優れているのであるが、よりその親和性の向上
を図るために、溶融スラグと粘度,比重等が近似するよ
うな化学組成を有することが望ましい。This glass is superior in affinity to the melt of steelmaking slag (hereinafter simply referred to as "slag") to the crystalline borate compound, but in order to further improve the affinity, It is desirable to have a chemical composition that is similar in viscosity, specific gravity, etc. to the molten slag.
【0026】従って、前記ガラスは多くの場合、化学組
成としてB2O3:20〜50重量%、CaO(及び/又
はMgO):10〜40重量%、SiO2:10〜35
重量%およびNa2O:5〜20重量%の範囲にある。Therefore, the glass often has a chemical composition of B 2 O 3 of 20 to 50% by weight, CaO (and / or MgO) of 10 to 40% by weight, and SiO 2 of 10 to 35%.
Wt% and Na 2 O: in the range of 5 to 20 wt%.
【0027】この範囲外であると粘性が高くなったり、
又はガラス化が困難となって、粉化防止剤の性能が劣化
する傾向にある。なお、不可避的に混入される不純物の
存在は当然に許容できることはいうまでもない。If it is out of this range, the viscosity becomes high,
Alternatively, vitrification tends to be difficult, and the performance of the powdering inhibitor tends to deteriorate. Needless to say, the presence of impurities that are inevitably mixed is naturally acceptable.
【0028】次に、本発明にかかる前記粉化防止剤はフ
レーク状を呈していることである。Next, the pulverization preventing agent according to the present invention is in the form of flakes.
【0029】この理由は、溶融スラグとの接触溶解が速
やかで均一にスラグ融液中に拡散できると共に、接触溶
解の際に発塵の発生が全く生じないことによる。The reason for this is that the contact dissolution with the molten slag is rapid and can be diffused uniformly in the slag melt, and no dust is generated during the contact dissolution.
【0030】ここで、本発明における“フレーク状”
は、スラグに対する溶融性,安全性および製造上の観点
から、アスペクト比が1:5以上、長径の平均径が5〜
25mmの範囲にあるものが好ましい。Here, the "flakes" in the present invention
Has an aspect ratio of 1: 5 or more and an average major axis diameter of 5 to 5 from the viewpoints of meltability to slag, safety, and manufacturing.
Those in the range of 25 mm are preferable.
【0031】本発明にかかる粉化防止剤は前記の如きガ
ラスフレーク状物を有効成分とするが、必要に応じ該ガ
ラスの砂状粉末を併用することもできる。The anti-dusting agent according to the present invention contains the glass flakes as described above as an active ingredient, but a sandy powder of the glass may be used together if necessary.
【0032】次に、前記粉化防止剤はガラス組成として
B2O3:20〜50重量%、CaO(及び/又はMg
O):10〜40重量%、SiO2:10〜35重量%
およびNa2O:5〜20重量%となるようにホウ素、
カルシウム(及び/又はマグネシウム)、珪素およびナ
トリウムの1種又は2種以上を含有する原料を配合し、
次いで得られる調合物を加熱溶液した後、該融液をフレ
イカーに流下し、次いで固化および粒度調整することに
より製造することができる。Next, the pulverization preventing agent has a glass composition of B 2 O 3 : 20 to 50% by weight, CaO (and / or Mg).
O): 10 to 40% by weight, SiO 2 : 10 to 35% by weight
And Na 2 O: boron so as to be 5 to 20% by weight,
A raw material containing one or more of calcium (and / or magnesium), silicon and sodium is blended,
The resulting formulation can then be heated to a solution before being made to flow by flowing the melt through a flaker, followed by solidification and particle size adjustment.
【0033】ホウ素原料として例えば前記したような、
ホウ酸、ホウ酸ソーダの如き化成品又はコレマナイト
(colemanite)(Ca2B6O11・5H
2O)、ウレキサイト(ulexite)(NaCaB5
O9・8H2O)、チンカル(tincal)(Na2B4
O7・10H2O)、カーナイト(kernite)(N
a2B4O7・4H2O)の如きホウ酸塩鉱物などがあげら
れる。As the boron raw material, for example, as described above,
Boric acid, such as chemicals or colemanite boric acid soda (colemanite) (Ca 2 B 6 O 11 · 5H
2 O), urexite (NaCaB 5
O 9 / 8H 2 O), tincal (Na 2 B 4
O 7 · 10H 2 O), carnite (kernite) (N
such as a 2 B 4 O 7 · 4H 2 O) such as borate minerals and the like.
【0034】カルシウム原料としては石灰石,消石灰,
生石灰,珪酸カルシウムなどがあげられ、マグネシウム
原料としてはカルシウム源からの不可避的に混入される
ものでよいが、マグネシア,ドロマイト,方解石などが
あげられる。珪素原料としては珪石,珪砂,珪華,珪酸
アルミニウム,珪酸カルシウムなどであり、ナトリウム
原料としては、ソーダ灰,珪酸ナトリウムガラスなどが
あげられる。As the calcium raw material, limestone, slaked lime,
Quick lime, calcium silicate, etc. may be mentioned. Magnesia, dolomite, calcite, etc. may be mentioned as the magnesium raw material which may be inevitably mixed from a calcium source. The silicon raw material is silica stone, silica sand, silica, aluminum silicate, calcium silicate, etc., and the sodium raw material is soda ash, sodium silicate glass and the like.
【0035】これらの原料を適宜選択してガラス組成と
して前記範囲になるように調合し、所望の溶融炉に投入
して加熱溶融する。溶融炉としては、石油炉,ガス炉,
コークス炉又は電気炉などがあるが、コストの面で石油
炉又はコークス炉が望ましい。These raw materials are appropriately selected and compounded so that the glass composition falls within the above range, and the mixture is put into a desired melting furnace and heated and melted. As a melting furnace, oil furnace, gas furnace,
Although there are coke ovens, electric ovens, etc., an oil or coke oven is preferable in terms of cost.
【0036】次いで、融液を、例えば10〜30mmφ
の出口よりフレイカー(水にて内部冷却した双ロール)
に流下し、薄い板状になったあめ状のガラスをベルトコ
ンベア上に流下して冷却固化させる。Next, the melt is filled with, for example, 10 to 30 mmφ.
From the exit of the flaker (double roll internally cooled with water)
Then, the candy-shaped glass in the form of a thin plate is flowed down on a belt conveyor to be cooled and solidified.
【0037】次いで、ベルトコンベアから固化したガラ
スを容器中へ落下させ、上記のような大きさのフレーク
状ガラスとなるように粉砕して本発明を得ることができ
る。Next, the solidified glass is dropped from the belt conveyor into a container and crushed to obtain a flake-shaped glass having the above-mentioned size, whereby the present invention can be obtained.
【0038】この本発明の製造工程においては、粒状化
する場合にも冷却する場合にも水を使用しないため、乾
燥工程を必要とせず、コスト面で非常に有利である。In the manufacturing process of the present invention, water is not used for granulation or cooling, so that a drying process is not required, which is very advantageous in terms of cost.
【0039】本発明において対象とするスラグは製鋼ス
ラグであるが、該スラグが冷却に際しあるいは経時変化
により崩壊し又は粉化する現象を生ずるようなものであ
り、一般的には塩基度CaO/SiO2(重量比)が
1.5以上のものである。The slag to be used in the present invention is a steelmaking slag, but it is one which causes a phenomenon such that the slag collapses or powders upon cooling or with the passage of time, and is generally CaO / SiO. 2 (weight ratio) is 1.5 or more.
【0040】また、本発明にかかる粉化防止剤を添加す
る態様は、添加後速やかに溶融スラグ中へ混合拡散する
ような方法を採れるものであれば特に限定する必要はな
い。例えば溶融スラグ表面に散布する方法、所望量を入
れた袋ごと投入する方法、圧力空気で移送して溶融スラ
グへ吹付けるように添加する方法、又は溶融スラグに添
加後不活性ガス(N2,Arガス)で攪拌する方法があ
げられる。Further, the mode of adding the dusting inhibitor according to the present invention is not particularly limited as long as a method of mixing and diffusing into the molten slag immediately after addition can be adopted. For example, a method of spraying on the surface of the molten slag, a method of charging the bag containing a desired amount, a method of transferring with pressurized air so as to be sprayed onto the molten slag, or an inert gas (N 2 , after addition to the molten slag, There is a method of stirring with Ar gas).
【0041】本発明にかかる粉化防止剤のスラグに対す
る添加量は、少なくともB2O3として0.1重量%であ
り、好ましくは0.2〜0.6重量%の範囲にある。約
0.1重量%を下回る場合は、スラグ粉化防止に不充分
であり、上限は主として経済上の理由から自ずと限定さ
れる。The amount of the dusting inhibitor according to the present invention added to slag is at least 0.1% by weight as B 2 O 3 , and preferably in the range of 0.2 to 0.6% by weight. If it is less than about 0.1% by weight, it is insufficient to prevent slag powdering, and the upper limit is naturally limited mainly for economic reasons.
【0042】以下本発明につき実施例にて具体的に説明
する。The present invention will be specifically described below with reference to examples.
【0043】[0043]
【実施例】実施例1 表1に示す配合割合(重量部)の原料配合物を25m3
容量の石油炉を用いて1200〜1250℃下で溶融し
た。 Example 1 25 m 3 of a raw material mixture having a mixing ratio (parts by weight) shown in Table 1 was used.
It was melted under a temperature of 1200 to 1250 ° C. using a petroleum furnace of a capacity.
【0044】[0044]
【表1】 [Table 1]
【0045】得られた融液を、20mmφの流出口より
内部水冷式双ロールのフレイカー中に流下させて板状に
したものを、可動しているベルトコンベア上に流出さ
せ、固化したものを粉砕して、表2に示す組成及び形状
のガラス化物を得た。The obtained melt was made to flow from an outlet of 20 mmφ into a breaker of an internal water-cooled twin roll to form a plate, which was flowed out on a movable belt conveyor and solidified. Then, a vitrified product having the composition and shape shown in Table 2 was obtained.
【0046】[0046]
【表2】 [Table 2]
【0047】これらのガラス化物をおのおの10kg宛
紙袋に密封し粉化防止剤試験試料とした。Each of these vitrified products was sealed in a paper bag of 10 kg and used as a test sample for an anti-dusting agent.
【0048】更に、ステンレス製鋼用電気炉(50t容
量)より製出された1回目出銑時のスラグ塩基度(Ca
O/SiO2=1.92)を取鍋よりスラグポットに除
滓する際、試験試料を約10kg紙袋のまま所定量同時
投入し、かかるスラグを放置冷却して固化した後に常温
に至るまでの状況を観察した。Further, the slag basicity (Ca) at the first tapping produced from an electric furnace for stainless steel (50 t capacity)
When removing the O / SiO 2 = 1.92) from the ladle to the slag pot, a predetermined amount of the test sample was simultaneously put in a paper bag of about 10 kg, and the slag was left to cool and solidify until it reached room temperature. I observed the situation.
【0049】試験時の条件は次の通りである。The conditions at the time of the test are as follows.
【0050】[0050]
【表3】 [Table 3]
【0051】試料添加に際し、いずれの実験においても
発塵,ガス発生は全く見られず、添加操作は安全であ
り、スラグポット内へのスラグ注湯時には良好な拡散混
合が得られた。When adding the sample, no dusting or gas generation was observed in any of the experiments, the adding operation was safe, and good diffusion mixing was obtained when pouring the slag into the slag pot.
【0052】更に試験時のスラグを常温まで放冷した後
に、状況を観察したところ、崩壊粉化現象は全く見られ
なかった。Further, when the condition was observed after the slag used in the test was allowed to cool to room temperature, no disintegration powdering phenomenon was observed at all.
【0053】尚、試験後のスラグ組成(重量%)は次の
通りであった。The slag composition (% by weight) after the test was as follows.
【0054】[0054]
【表4】 [Table 4]
【0055】なお、このスラグ自体は冷却すると自己崩
壊して粉化するものである。The slag itself self-disintegrates and powders when cooled.
【0056】また、A,B,Cの試料添加のスラグ(改
質後)と無添加のスラグ(改質前)を以下の処理条件で
オートクレーブ処理によるスラグの崩壊率測定を行っ
た。Further, the slag disintegration rate was measured by autoclaving the slags (after reforming) and the slags without addition (before reforming) of samples A, B, and C under the following treatment conditions.
【0057】処理条件:試料スラグ破砕後粒径10〜2
5mmに粒度調整し、これを200℃,20kg/cm
2,3時間オートクレーブ内に保持し、次いで乾燥した
後、ふるい分け10mm未満の粒径のものを崩壊物とし
た。Treatment conditions: Particle size 10 to 2 after crushing sample slag
The particle size is adjusted to 5 mm, and this is 200 ° C, 20 kg / cm
It was kept in the autoclave for a few hours and then dried, and then sieved to obtain a disintegrated material having a particle size of less than 10 mm.
【0058】上記オートクレーブ処理後の崩壊物の割合
(%)を示すThe proportion (%) of the disintegrated product after the autoclave treatment is shown.
【0059】[0059]
【表5】 [Table 5]
【0060】比較例1 実施例1において、粉化防止剤として溶融スラグに対し
ホウ砂(Na2B4O7・10H2O)(B2O3:37.0
0重量%,Na2O:16.5重量%)(0.2〜0.
4mmのものが55%)を12kg/tスラグ、ビニー
ル袋ごと投入したところ、激しい飛散と吹き上げを生じ
未溶解の塊りが生じたので、投入を中止せざるを得なか
った。 Comparative Example 1 In Example 1, borax (Na 2 B 4 O 7 · 10H 2 O) (B 2 O 3 : 37.0) was added to the molten slag as an anti-dusting agent.
0 wt%, Na 2 O: 16.5 wt%) (0.2-0.
When 12 kg / t slag and vinyl bag were charged together with 55 mm of 4 mm), vigorous scattering and blowing up occurred and undissolved lumps were generated, so the injection had to be stopped.
【0061】[0061]
1)本発明品は、ガラス化したスラグ粉化防止剤である
ために炭酸ガス,水蒸気等の熱分解気化熱、転移熱等溶
融に伴なう吸熱量が小さく、特にフレーク状であるため
に溶融速度が従来のものに比べ極めて速い。1) Since the product of the present invention is a vitrification inhibitor for slag powder, it has a small heat absorption amount due to melting such as thermal decomposition vaporization heat of carbon dioxide gas and water vapor, and transition heat, and is particularly flaky. The melting rate is much faster than the conventional one.
【0062】2)溶融スラグに対する粘度,密度等の差
の小さい親和性に富んだ化学組成に設計してある為に、
従来品に比べ本発明品は拡散混合の効果が極めて大き
い。2) Since the chemical composition is designed to have a high affinity with a small difference in viscosity, density, etc. with respect to the molten slag,
Compared with the conventional product, the product of the present invention has an extremely large effect of diffusion mixing.
【0063】3)ガラス化した無水のスラグ粉化防止剤
であるため、脱ガス反応を起こさず、更にフレーク状の
大きさであることから、溶融スラグへの添加時に吹き上
げ,飛塵等により作業環境を悪化させることがない。3) Since it is a vitrified anhydrous slag dusting inhibitor, it does not cause a degassing reaction and has a flake-like size. Therefore, when added to the molten slag, it is blown up and works by dust. It does not make the environment worse.
【0064】4)本発明の製造工程においては、水を使
用しないため、乾燥工程を必要とせず、簡便に且つ安価
に製造することができる。4) Since water is not used in the production process of the present invention, a drying process is not required and the production can be carried out easily and at low cost.
Claims (5)
有効成分とする製鋼スラグの粉化防止剤。1. An anti-dusting agent for steelmaking slag, which comprises a flake-shaped alkali borosilicate glass as an active ingredient.
2O3として20〜50重量%含有する請求項1に記載の
製鋼スラグの粉化防止剤。2. Alkali borosilicate glass contains boron as B
The powdering inhibitor for steelmaking slag according to claim 1, which contains 20 to 50% by weight as 2 O 3 .
してB2O3:20〜50重量%、MO:10〜40重量
%(但し、MはCa,Mgを表す。)、SiO2:10
〜35重量%およびNa2O:5〜20重量%を含有す
る請求項1又は2に記載の製鋼スラグの粉化防止剤。3. The alkali borosilicate glass has a chemical composition of B 2 O 3 : 20 to 50% by weight, MO: 10 to 40% by weight (wherein M represents Ca and Mg), and SiO 2 : 10.
The pulverization inhibitor for steelmaking slag according to claim 1 or 2, which comprises ˜35 wt% and Na 2 O: 5 to 20 wt%.
比が1:5以上,長径の平均径が5〜20mmのフレー
ク状を呈する請求項1乃至3のいずれかに記載の製鋼ス
ラグの粉化防止剤。4. The pulverization inhibitor for steelmaking slag according to claim 1, wherein the alkali borosilicate glass has a flake shape with an aspect ratio of 1: 5 or more and an average major axis diameter of 5 to 20 mm. .
量%、MO:10〜40重量%(但し、MはCa,Mg
を表す。)、SiO2:10〜35重量%およびNa
2O:5〜20重量%となるようにホウ素、カルシウム
(及び/又はマグネシウム)、珪素およびナトリウムの
1種又は2種以上含有する原料を調合し、次いで得られ
る調合物を加熱溶融した後、該融液をフレイカーに流下
し、次いで固化および粒度調整して、フレーク状のホウ
珪酸アルカリガラスを有効成分とする製鋼スラグの粉化
防止剤を製造する方法。5. B 2 O 3 as a glass composition: 20 to 50% by weight, MO: 10 to 40% by weight (where M is Ca, Mg)
Represents ), SiO 2 : 10-35 wt% and Na
2 O: a raw material containing one or more of boron, calcium (and / or magnesium), silicon and sodium in an amount of 5 to 20% by weight is prepared, and then the obtained composition is melted by heating, A method for producing an anti-dusting agent for steelmaking slag containing flake-shaped alkali borosilicate glass as an active ingredient by allowing the melt to flow down to a flaker, followed by solidification and particle size adjustment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6193790A JPH0834643A (en) | 1994-07-27 | 1994-07-27 | Steelmaking slag pulverization inhibitor and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6193790A JPH0834643A (en) | 1994-07-27 | 1994-07-27 | Steelmaking slag pulverization inhibitor and method for producing the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0834643A true JPH0834643A (en) | 1996-02-06 |
Family
ID=16313840
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6193790A Withdrawn JPH0834643A (en) | 1994-07-27 | 1994-07-27 | Steelmaking slag pulverization inhibitor and method for producing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0834643A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011105519A (en) * | 2009-11-12 | 2011-06-02 | Sanyo Special Steel Co Ltd | Rapid aging method for steel slag |
| CN111548008A (en) * | 2020-05-25 | 2020-08-18 | 广东德仁光电科技有限公司 | Preparation method of ADF glass and ADF glass prepared by adopting same |
| CN116789426A (en) * | 2023-06-27 | 2023-09-22 | 江苏集萃功能材料研究所有限公司 | Method for coupling mineralization resource utilization of modified steel slag and application of method |
-
1994
- 1994-07-27 JP JP6193790A patent/JPH0834643A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011105519A (en) * | 2009-11-12 | 2011-06-02 | Sanyo Special Steel Co Ltd | Rapid aging method for steel slag |
| CN111548008A (en) * | 2020-05-25 | 2020-08-18 | 广东德仁光电科技有限公司 | Preparation method of ADF glass and ADF glass prepared by adopting same |
| CN116789426A (en) * | 2023-06-27 | 2023-09-22 | 江苏集萃功能材料研究所有限公司 | Method for coupling mineralization resource utilization of modified steel slag and application of method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20011002 |