JP3021946B2 - Cooling method for high temperature steelmaking slag - Google Patents

Cooling method for high temperature steelmaking slag

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Publication number
JP3021946B2
JP3021946B2 JP9769992A JP9769992A JP3021946B2 JP 3021946 B2 JP3021946 B2 JP 3021946B2 JP 9769992 A JP9769992 A JP 9769992A JP 9769992 A JP9769992 A JP 9769992A JP 3021946 B2 JP3021946 B2 JP 3021946B2
Authority
JP
Japan
Prior art keywords
slag
watering
pressure
steam
temperature
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 - Fee Related
Application number
JP9769992A
Other languages
Japanese (ja)
Other versions
JPH05295409A (en
Inventor
敏 田淵
尾花保雄
松尾慎二
司 柏原
工藤俊昭
伊美哲生
純啓 堀
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
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Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP9769992A priority Critical patent/JP3021946B2/en
Publication of JPH05295409A publication Critical patent/JPH05295409A/en
Application granted granted Critical
Publication of JP3021946B2 publication Critical patent/JP3021946B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/066Receptacle features where the slag is treated
    • C21B2400/068Receptacle features where the slag is treated with a sealed or controlled environment
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

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  • Manufacture Of Iron (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、高温製鋼スラグの冷却
処理方法に関するものである。製鋼スラグは一般に、C
aO分を含み、f.CaOの形態で1%以上存在してい
る。この200℃以上の高温製鋼スラグを固化させた
後、密閉容器内の目皿上に上方装入して、0.5〜4m
の層厚に充填し密閉後、このスラグ充填層の上方から5
〜30ton/hrm2 の散水密度で冷却水を散水し、
密閉容器中でスラグの水和反応を促進すると同時に破砕
効果を得る手段を提供しようとするものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cooling high-temperature steelmaking slag. Steelmaking slag is generally C
aO content, f. 1% or more is present in the form of CaO. After solidifying this high-temperature steelmaking slag of 200 ° C. or higher, it is charged upward onto a plate in a closed container, and 0.5 to 4 m
After filling and sealing, the slag-filled layer is
Watering the cooling water at a watering density of 3030 ton / hrm 2 ,
An object of the present invention is to provide a means for promoting the hydration reaction of slag in a closed container and at the same time obtaining a crushing effect.

【0002】[0002]

【従来の技術】通常の製鋼スラグ処理においては、まず
スラグを土場又は鉄板上に放流して、固化冷却を行う。
2. Description of the Related Art In a usual steelmaking slag treatment, slag is first discharged onto a pit or an iron plate to perform solidification and cooling.

【0003】冷却完了後、破砕機にて必要粒度まで破砕
し、破砕されたスラグは磁選機を通し鉄分を回収した
後、路盤材、埋め立て等に利用される。
[0003] After the cooling is completed, the crushed slag is crushed to a required particle size by a crusher, and the crushed slag is passed through a magnetic separator to recover iron, and then used for roadbed material, landfill, and the like.

【0004】しかしながら上記した冷却、破砕、磁選処
理は、粉塵が飛散し環境的に劣悪であり、特に冷却工程
では高熱下での作業も余儀無くされその作業は過酷なも
のとなっている。
However, the above-mentioned cooling, crushing, and magnetic separation treatments are environmentally inferior due to scattering of dust. Particularly in the cooling step, work under high heat is unavoidable, and the work is severe.

【0005】又、処理時間が長く、多工程であるため、
運転費、人件費等、処理費用がかさみ、更に敷地につい
ても膨大な面積が必要とされる。
In addition, since the processing time is long and the number of steps is large,
Processing costs such as operating costs and personnel costs are high, and a huge area is required for the site.

【0006】その上、処理後の製鋼スラグは水和反応物
を多く含むため、路盤材等に販売する場合は、0.5〜
3年程度、長期間ヤードに放置し、膨張性を低下させ安
定化させる事が必要である。そこで過去に、密閉容器中
で高温スラグに散水を行ってスラグを処理する発明が特
開昭55−110703号公報で紹介されている。これ
は密閉容器に装入した高温スラグに散水し、発生水蒸気
にて水和反応を促進してスラグを安定化させる方法であ
る。
[0006] In addition, since the steelmaking slag after the treatment contains a large amount of hydration reaction products, when sold as a roadbed material or the like, 0.5 to 0.5 to
It is necessary to leave it in a yard for a long period of about three years to reduce its inflation and stabilize it. Therefore, in the past, an invention in which high-temperature slag is sprinkled in a closed container to treat the slag has been introduced in Japanese Patent Application Laid-Open No. 55-110703. This is a method in which water is sprinkled on a high-temperature slag charged in a closed container, and hydration reaction is promoted by generated steam to stabilize the slag.

【0007】[0007]

【発明が解決しようとする課題】しかし上記発明は、長
時間の水和反応処理時間を用しても充分な水和反応を起
こさせる手段ではなく、しかも破砕効果が全く得られな
いため、水和反応処理後に破砕処理等の煩雑多工程の付
加が必要であり、設備費、処理コスト高、破砕処理時の
粉塵対策等の問題を抱えていた。
However, the above-mentioned invention is not a means for causing a sufficient hydration reaction even if a long hydration reaction treatment time is used, and furthermore, since no crushing effect is obtained, water It is necessary to add complicated and complicated steps such as crushing after the summation reaction, and there are problems such as high equipment costs, high processing costs, and measures against dust during crushing.

【0008】[0008]

【課題を解決するための手段】本発明は、上記課題を解
決するため、密閉処理を利用した水和反応を効果的に大
幅に促進させると同時に破砕効果が得られる冷却処理方
法を新たに見い出したものでありその特徴とする手段
は、密閉容器内の目皿上に高温製鋼スラグを上方装入し
て0.5〜4mの層厚に充填し密閉後、このスラグ充填
層の上方から5〜30ton/hrm2 の散水密度で冷
却水を散水し、前記散水によって発生した水蒸気または
同水蒸気と別途容器内に注入した水蒸気にて容器内圧力
を高めて容器内圧力とその保持時間との関係を(1)式
で定めてた範囲内に維持して処理することを特徴とする
高温製鋼スラグの冷却処理方法である。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention has newly found a cooling treatment method capable of effectively and greatly promoting a hydration reaction utilizing a sealing treatment and at the same time obtaining a crushing effect. The characteristic feature is that high-temperature steelmaking slag is charged above a plate in a closed vessel, filled to a thickness of 0.5 to 4 m, sealed, and then filled with slag from above the slag-filled layer by 5 mm. Cooling water is sprinkled at a sprinkling density of 3030 ton / hrm 2 , and the pressure in the container and the holding time are increased by increasing the pressure in the container with the steam generated by the watering or the steam and the steam separately injected into the container. Is maintained within the range defined by the equation (1).

【0009】 3.50≧P0.6 ×T0.4 ≧1.48…(1) P≦15 T≦1 但し P:水蒸気圧力(kg/cm2 ) T:処理時間
(hr) 前記特徴の他に、散水を間欠的に行うこと、スラグ温度
200℃以下にて散水を停止し、その後圧力保持中に間
欠散水を行うこと等も特徴とする。
3.50 ≧ P 0.6 × T 0.4 ≧ 1.48 (1) P ≦ 15 T ≦ 1 where P: steam pressure (kg / cm 2 ) T: treatment time (hr) It is also characterized by intermittent watering, stopping watering at a slag temperature of 200 ° C. or lower, and then intermittently watering while maintaining the pressure.

【0010】[0010]

【作用】前記本発明の処理方法は、水和反応を効果的に
かつ迅速に促進されるため、スラグの安定化が短時間で
完了するだけでなく、スラグの自己破砕までも行わせ、
従来の破砕工程を省略し工程と設備の簡素化を可能とす
る。この自己破砕は、散水の冷却促進に繋がる相乗効果
を生ましめ、スラグの冷却速度は大幅に増大し、短時間
の冷却を可能とする。以上の処理工程の時間短縮、工程
の省略化、簡素化は、同時に省力化、処理コストの低
減、そして粉塵対策の軽減を可能とし、かつプロセスの
自動化も容易にするものであり以下にその作用を詳細に
説明する。
According to the treatment method of the present invention, the hydration reaction is effectively and rapidly promoted, so that not only the slag stabilization is completed in a short time, but also the slag is self-crushed,
The conventional crushing process is omitted, and the process and equipment can be simplified. This self-crushing produces a synergistic effect that promotes cooling of water spray, greatly increases the cooling rate of slag, and enables short-time cooling. The above-mentioned shortening of processing time, elimination and simplification of the processing simultaneously enable labor saving, reduction of processing cost, reduction of dust measures, and easy automation of the process. Will be described in detail.

【0011】製鋼スラグ中にはf.CaOが存在し、水
又は水蒸気と反応して以下の式に示す水和反応を起こ
す。
During the steelmaking slag, f. CaO is present and reacts with water or steam to cause a hydration reaction represented by the following formula.

【0012】CaO+H2 O=Ca(OH)2 従来から高圧にてH2 Oを供給すると水和反応が促進す
る事は言われている。しかしながら、単に高圧H2 O中
に保持するだけでは、水和反応は依然遅く、特開昭55
−110703の方法のように水蒸気をスラグ間隔に長
時間・高温下で通過流動しながら保持しても、ある程度
の促進は得られるが、未反応部分が非常に多い、従って
この処理後に別途広大なスラグヤードに搬出して大気に
露出させ長期間の養生(エージング)を必要としてい
た。
CaO + H 2 O = Ca (OH) 2 It has been conventionally said that supplying H 2 O at a high pressure accelerates the hydration reaction. However, the hydration reaction is still slow by simply keeping the solution in high-pressure H 2 O.
Although a certain degree of promotion can be obtained even when steam is passed and maintained at a high temperature for a long time at a slag interval as in the method of -110703, a large amount of unreacted parts is obtained, and therefore, after this treatment, it is separately vast. It was transported to a slag yard and exposed to the atmosphere, requiring long-term curing (aging).

【0013】本発明において、前記装入充填した高温ス
ラグ層の上方から散水して高温スラグに散水密度5〜3
0ton/hrm2 を与え、これで自ら発生した水蒸気
または、この水蒸気と他から注入した水蒸気にて、容器
内を高圧に保持し、以下の条件にてスラグを処理する
と、図1、図2に示す様に、スラグの自己破砕が得られ
ると同時に該自己破砕により水和反応開始表面領域が急
増して水和反応が想像以上に迅速に促進される。
[0013] In the present invention, water is sprayed from above the charged and filled high-temperature slag layer to spray the high-temperature slag with a watering density of 5 to 3.
When 0 ton / hrm 2 is given and the inside of the container is kept at a high pressure with steam generated by itself or this steam and steam injected from another, and the slag is treated under the following conditions, FIG. 1 and FIG. As shown, self-crushing of the slag is obtained, and at the same time, the self-crushing rapidly increases the surface area of the hydration reaction start, thereby promoting the hydration reaction more rapidly than expected.

【0014】 3.50≧P0.6 ×T0.4 ≧1.48…(1) P≦15 T≦1 但し P:水蒸気圧力(kg/cm2 ) T:処理時間
(hr) 散水密度を5ton/hrm2 以上であると0.5m以
上の充填層においては、スラグに水が均一にかかり、チ
ャンネリング(偏流)をおこしにくくなる。そのため容
器内の全てのスラグは急冷され、同時に熱収縮で亀裂を
生じる。水和反応は発熱反応であるため高温では反応が
遅いが、急冷により反応速度が向上する。又、亀裂が生
じた事によりスラグ中のf.CaOとH2 Oの接触面積
が広がり反応量が増大する。又、H2 Oを液体でスラグ
に接触させるため、充分に反応物としてのH2 Oの供給
を可能とし、供給不足による反応の停滞も防止してい
る。また逆に散水密度は、30ton/hrm2 を超え
て散水しても、スラグの冷却速度に変化なく、単に容器
内の蒸気を冷却する作用のみが行われるため、熱ロスに
よる蒸気補給量増を余儀無くされる。そのため散水密度
は、30ton/hrm2 以下が望ましい。
3.50 ≧ P 0.6 × T 0.4 ≧ 1.48 (1) P ≦ 15 T ≦ 1 where P: steam pressure (kg / cm 2 ) T: treatment time (hr) Sprinkling density is 5 ton / hrm If it is 2 or more, in a packed bed of 0.5 m or more, water is uniformly applied to the slag, and channeling (drift) becomes difficult to occur. Therefore, all the slag in the container is quenched, and at the same time, cracks due to heat shrinkage. The hydration reaction is exothermic, so the reaction is slow at high temperatures, but the reaction speed is improved by rapid cooling. In addition, f. The contact area between CaO and H 2 O increases, and the reaction amount increases. Further, since H 2 O is brought into contact with the slag with a liquid, it is possible to sufficiently supply H 2 O as a reactant, thereby preventing stagnation of the reaction due to insufficient supply. Conversely, even if the water spray density exceeds 30 ton / hrm 2 , the cooling rate of the slag does not change and only the function of cooling the steam in the container is performed. I will be forced. Therefore, the watering density is desirably 30 ton / hrm 2 or less.

【0015】圧力と時間については、上記に示した領域
に限定する事で、自己破砕現象が起き、この自己崩壊現
象がさらに水和反応を促進させる。すなわち、この自己
破砕は、f.CaOとH2 Oの接触面積を広げ水和反応
速度の向上を増長させるだけでなく、スラグとH2 Oの
接触面積を広げ、スラグ温度を低下させる事で更に水和
反応速度の向上を増長させる。
By limiting the pressure and time to the above-mentioned regions, a self-crushing phenomenon occurs, and this self-disintegration phenomenon further promotes the hydration reaction. That is, this self-crushing is carried out by f. In addition to increasing the contact area between CaO and H 2 O to increase the hydration reaction rate, the contact area between slag and H 2 O is increased and the slag temperature is further reduced to further increase the hydration reaction rate. Let it.

【0016】一方、スラグ温度は低下させすぎても反応
速度は遅くなる。水蒸気を高圧にて保持する事は、高圧
による反応速度向上だけでなく、飽和水蒸気温度が維持
されるため、最適のスラグ温度維持にも効果を発揮して
いる。
On the other hand, if the slag temperature is too low, the reaction rate will be low. Holding steam at a high pressure not only improves the reaction rate due to the high pressure, but also maintains the saturated steam temperature, which is effective in maintaining the optimum slag temperature.

【0017】規定に高圧を保持するため、自己発生蒸気
にて保持が不可能になった時は、他から水蒸気を注入し
て圧力を保持する。圧力保持の観点から5ton/hr
2以上の散水は、スラグ平均温度が200℃以下にな
ったら散水を中断する事が望ましい。
In order to maintain a prescribed high pressure, when it becomes impossible to maintain the self-generated steam, steam is injected from another source to maintain the pressure. 5ton / hr from the viewpoint of pressure maintenance
It is desirable to suspend watering of m 2 or more when the average slag temperature becomes 200 ° C. or less.

【0018】次に、間欠散水の効果について述べる。他
からの水蒸気注入量をミニマムにする必要が生じた時は
散水密度を維持し、絶対散水量を減らす事が望ましい。
その為には、スラグの表面温度が200℃以下になった
ら一旦散水を中断する。するとスラグ内部の熱が表面に
移動する復熱現象が起き、その段階で散水を再開する。
Next, the effect of intermittent watering will be described. When it becomes necessary to minimize the amount of water vapor injected from others, it is desirable to maintain the watering density and reduce the absolute watering amount.
For that purpose, once the surface temperature of the slag becomes 200 ° C. or less, watering is temporarily stopped. Then, a recuperation phenomenon occurs in which heat inside the slag moves to the surface, and watering is resumed at that stage.

【0019】以上の作用を繰り返す方法、すなわち間欠
散水を行うならば、絶対散水量が減り効率的な水和反応
と自己破砕処理が達成できる。ちなみに間欠の間隔は1
分以上が望ましい。更に間欠の場合、熱収縮による亀裂
増大効果を最大限享受でき、それによる水和反応領域が
激増してスラグ充填層全体の水和反応完了が迅速になさ
れる。
If a method of repeating the above operation, that is, intermittent watering, is performed, the absolute watering amount is reduced, and efficient hydration reaction and self-crushing can be achieved. By the way, the intermittent interval is 1
Minutes or more is desirable. Furthermore, in the case of intermittent operation, the effect of increasing cracks due to heat shrinkage can be enjoyed to the utmost, whereby the hydration reaction region increases drastically, and the hydration reaction of the entire slag packed bed is completed quickly.

【0020】処理の後半での圧力保持中においては、ス
ラグの平均温度が200℃以下になったならば、散水を
中断し、圧力保持を行った方が良い事は先に述べた。た
だ、水蒸気圧力保持中に水和反応を促進させているた
め、圧力保持に支障がない程度に間欠的に散水を行い、
液体としてのH2 Oを供給してやる方が水和反応を最大
限、促進させる事が出来る。
As mentioned earlier, during the pressure holding in the latter half of the treatment, if the average temperature of the slag becomes 200 ° C. or less, it is better to stop watering and hold the pressure. However, since the hydration reaction is promoted while maintaining the steam pressure, water is intermittently sprinkled to such an extent that there is no problem in maintaining the pressure.
By supplying H 2 O as a liquid, the hydration reaction can be promoted to the maximum.

【0021】以上述べてきた条件の処理を可能とする設
備について、図3に示す。特開昭55−110703に
て開示された設備において、5ton/hrm2 以上の
散水密度を満たす散水機構を供え、かつ他から水蒸気を
注入出来る様になっている。本設備を用いれば、上記し
たスラグ処理が可能である。
FIG. 3 shows equipment capable of processing under the conditions described above. The equipment disclosed in Japanese Patent Application Laid-Open No. 55-110703 is provided with a watering mechanism that satisfies a watering density of 5 ton / hrm 2 or more, and is capable of injecting water vapor from other sources. If this facility is used, the above-mentioned slag processing is possible.

【0022】[0022]

【実施例】温度800℃、平均粒径が100mm、最大
粒径が500mmの高温スラグ(組成:(%CaO)=
50%,(%SiO2 )=15,(%MnO)=12
%,(%T.Fe)=12%,f.CaOの形態で5
%)を図3に示す設備の下部に目皿を持つ鋼板容器1
に、高さ1m充填し、その容器を2の圧力容器中に3部
を開けて挿入する。3部を密閉した後、ポンプ4と流量
調整弁5を用いて、給水タンク6より注入ノズル7を通
じて圧力容器内へ水を注入する。注入された水は高温ス
ラグと接触し、蒸気となり、圧力容器内は高圧化され
る。その圧力を圧力計8で検知し、その圧力は圧力調整
弁9で調整される。圧力が不足する場合は10のライン
から蒸気を注入する。蒸気が過剰な場合は蒸気放散塔1
1から放散される。以上の処理を表1の処理水準にて実
施した。同表に処理後の細粒化スラグの平均粒度を示
す。本表によれば、本発明の条件範囲内で処理したもの
は、比較的低温まで冷却が図れ、自己破砕をおこした。
また間欠散水をしたものは、さらに後工程の鉄分回収の
ための磁力選鉱工程に必要な細かい粒度まで自己破砕を
おこした。また水和反応の残存代は大幅に低減してい
た。
EXAMPLE High-temperature slag having a temperature of 800 ° C., an average particle size of 100 mm and a maximum particle size of 500 mm (composition: (% CaO) =
50%, (% SiO 2 ) = 15, (% MnO) = 12
%, (% T.Fe) = 12%, f. 5 in the form of CaO
%) Is a steel plate container 1 having a perforated plate at the bottom of the equipment shown in FIG.
Is filled with a height of 1 m, and the container is inserted into the pressure vessel of 2 with opening 3 parts. After sealing the three parts, water is injected into the pressure vessel from the water supply tank 6 through the injection nozzle 7 by using the pump 4 and the flow control valve 5. The injected water comes into contact with the high-temperature slag and turns into steam, and the pressure inside the pressure vessel is increased. The pressure is detected by a pressure gauge 8, and the pressure is adjusted by a pressure adjusting valve 9. If pressure is insufficient, steam is injected from line 10. If the steam is excessive, steam stripper 1
Dissipated from 1. The above processing was performed at the processing level shown in Table 1. The table shows the average particle size of the refined slag after the treatment. According to this table, those treated within the condition range of the present invention could be cooled to a relatively low temperature and self-crushed.
The water that had been intermittently sprayed was further self-crushed to a fine particle size necessary for the magnetic separation process for iron recovery in the subsequent process. Also, the residual cost of the hydration reaction was significantly reduced.

【0023】[0023]

【表1】 [Table 1]

【0024】[0024]

【発明の効果】本発明のスラグ処理を行う事で、高温の
スラグは短時間で冷却され、その過程で自己破砕も行わ
れる。処理後スラグは大幅に水和反応が促進しており、
スラグの安定化も大幅に促進している。
By performing the slag treatment of the present invention, high-temperature slag is cooled in a short time, and self-crushing is performed in the process. After treatment, the hydration reaction of slag is greatly accelerated,
Slag stabilization is also greatly promoted.

【0025】以上の作用により、冷却工程の短縮、破砕
工程の簡素化又は省略、そしてそれに伴い、破砕以降の
磁力選鉱工程等を冷却工程と統合する事も可能となる。
工程の短縮、省略、統合は、発塵源の減少、高熱作業場
所の低減、人員の削減、処理費用の削減、自動化の容易
化等、二次的な効果も可能となる。スラグの安定化の大
幅促進は、ヤードでのエージング時間も更に短縮でき、
ヤードの在庫削減、そしてそれに伴う発塵源の低減効果
が得られる。
By the above operation, the cooling step can be shortened, the crushing step can be simplified or omitted, and the magnetic separation process and the like after the crushing can be integrated with the cooling step.
Shortening, omitting, and integrating processes can also have secondary effects, such as fewer sources of dust, fewer hot workplaces, fewer personnel, lower processing costs, and easier automation. Significant promotion of slag stabilization can further reduce aging time in the yard,
The yard inventory can be reduced, and the resulting reduction of dust sources can be achieved.

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

【図1】散水密度と処理後スラグ径の関係Fig. 1 Relationship between watering density and slag diameter after treatment

【図2】容器内圧力およびその保持時間による破砕条件
について
Fig. 2 Crushing conditions depending on the pressure in the vessel and the holding time

【図3】本発明のスラグ冷却処理装置FIG. 3 is a slag cooling treatment apparatus of the present invention.

【図4】(A)は、従来技術の処理パターンを示す図。
(B)は、本発明の処理パターンを示す図。(C)は、
本発明の処理パターン、間欠散水有りを示す図。(D)
は、本発明の処理パターン、スラグ温度200℃で散水
中止パターンを示す図。
FIG. 4A is a diagram showing a processing pattern according to the related art.
(B) is a diagram showing a processing pattern of the present invention. (C)
The figure which shows the processing pattern of this invention, and the presence of intermittent watering. (D)
FIG. 3 is a diagram showing a treatment pattern of the present invention, a watering stop pattern at a slag temperature of 200 ° C.

【符号の説明】[Explanation of symbols]

1…容器 2…圧力容器 3…開閉部 4…ポンプ 5…流量調整弁 6…給水タンク 7…注水ノズル 8…圧力計 9…圧力調整弁 10…蒸気注入ライン 11…蒸気放散塔 DESCRIPTION OF SYMBOLS 1 ... Container 2 ... Pressure container 3 ... Opening / closing part 4 ... Pump 5 ... Flow control valve 6 ... Water supply tank 7 ... Water injection nozzle 8 ... Pressure gauge 9 ... Pressure control valve 10 ... Steam injection line 11 ... Steam release tower

フロントページの続き (72)発明者 柏原 司 大分市大字西ノ洲1番地 新日本製鐵株 式会社大分製鐵所内 (72)発明者 工藤俊昭 大分市大字西ノ洲1番地 新日本製鐵株 式会社大分製鐵所内 (72)発明者 伊美哲生 大分市大字西ノ洲1番地 新日本製鐵株 式会社大分製鐵所内 (72)発明者 堀 純啓 大分市大字西ノ洲1番地 新日本製鐵株 式会社大分製鐵所内 (58)調査した分野(Int.Cl.7,DB名) F27D 15/00 - 15/02 C21B 3/06 - 3/08 C21C 7/00 Continuing from the front page (72) Inventor Tsukasa Kashiwara Oita-shi, 1 Nishinosu, Nippon Steel Corporation Oita Works, Ltd. Inside the steelworks (72) Inventor Tetsuo Imi Oita Nishi-no-Shi 1 Oita City Nippon Steel Corporation Oita Steel Works (72) Inventor Hori Sumiki 1 Oita-shi Oaza Nishi-nosu 1 Nippon Steel Corporation Oita Steel In-house (58) Field surveyed (Int.Cl. 7 , DB name) F27D 15/00-15/02 C21B 3/06-3/08 C21C 7/00

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 固化した高温の製鋼スラグを密閉容器内
の目皿上に充填し、このスラグ充填層の上方から散水し
冷却する高温製鋼スラグの冷却処理方法において、 散水密度を5〜30ton/hrm2 にて冷却水を散水
し、前記散水によって発生した水蒸気または同水蒸気と
別途容器内に注入した水蒸気にて容器内圧力を高めて容
器内圧力とその保持時間との関係を下記(1)式で定め
てた範囲内に維持して処理することを特徴とする高温製
鋼スラグの冷却処理方法 3.50≧P0.6 ×T0.4 ≧1.48…(1) P≦15 T≦1 但し P:水蒸気圧力(kg/cm2 ) T:処理時間
(hr)
1. A method for cooling a high-temperature steelmaking slag in which solidified high-temperature steelmaking slag is filled into a perforated plate in an airtight container, and water is sprayed and cooled from above the slag-filled layer. Cooling water is sprinkled at hr 2 , and the pressure in the container is increased by the steam generated by the watering or the steam and the steam separately injected into the container. 3. A cooling treatment method for high-temperature steelmaking slag characterized by maintaining and treating within the range defined by the formula: 3.50 ≧ P 0.6 × T 0.4 ≧ 1.48 (1) P ≦ 15 T ≦ 1 : Steam pressure (kg / cm 2 ) T: Processing time (hr)
【請求項2】 散水を間欠的に行うことを特徴とする請
求項1記載の高温製鋼スラグの冷却処理方法。
2. The method for cooling a high-temperature steelmaking slag according to claim 1, wherein watering is performed intermittently.
【請求項3】 スラグ温度200℃以下にて散水を停止
し、その後圧力保持中に間欠散水を行うことを特徴とす
る請求項1記載の高温製鋼スラグの冷却処理方法。
3. The method for cooling a high-temperature steelmaking slag according to claim 1, wherein watering is stopped at a slag temperature of 200 ° C. or lower, and then intermittent watering is performed while maintaining the pressure.
JP9769992A 1992-04-17 1992-04-17 Cooling method for high temperature steelmaking slag Expired - Fee Related JP3021946B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9769992A JP3021946B2 (en) 1992-04-17 1992-04-17 Cooling method for high temperature steelmaking slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9769992A JP3021946B2 (en) 1992-04-17 1992-04-17 Cooling method for high temperature steelmaking slag

Publications (2)

Publication Number Publication Date
JPH05295409A JPH05295409A (en) 1993-11-09
JP3021946B2 true JP3021946B2 (en) 2000-03-15

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ID=14199183

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Country Status (1)

Country Link
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Also Published As

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