JPH1172291A - Method of collecting dust in ore discharge part of sintering equipment - Google Patents

Method of collecting dust in ore discharge part of sintering equipment

Info

Publication number
JPH1172291A
JPH1172291A JP23368397A JP23368397A JPH1172291A JP H1172291 A JPH1172291 A JP H1172291A JP 23368397 A JP23368397 A JP 23368397A JP 23368397 A JP23368397 A JP 23368397A JP H1172291 A JPH1172291 A JP H1172291A
Authority
JP
Japan
Prior art keywords
dust
temperature
mist
gas
ore
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.)
Withdrawn
Application number
JP23368397A
Other languages
Japanese (ja)
Inventor
Chikao Ono
力生 小野
Kanji Aizawa
完二 相沢
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP23368397A priority Critical patent/JPH1172291A/en
Publication of JPH1172291A publication Critical patent/JPH1172291A/en
Withdrawn legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To reduce quantity of dust sucked into a dust collector by spraying a mist to an ore discharge part in coincidence with production of the dust at the time of crush of sintered ore when a large amount of the dust produced at the time of crushing sintered ore of high temperature by a crusher is collected by a dust collector provided above the crusher in the ore discharge part of sintering equipment. SOLUTION: Lumps of sintered ore 1 falling from a pallet 2 for conveying the sintered ore 1 is crushed by a crusher 3. By this crushing a large volume of high temperature gas and dust are produced and temperature of an atmosphere starts rising. The temperature of the atmosphere rising due to production of the high temperature gas is detected by a thermometer 8 and when the temperature reaches a specified temperature, a mist is sprayed from a mist nozzle 7. As a result, the temperature of the atmosphere is lowered and the volume of the gas is reduced. A large amount of the dust sucked by a dust collection hood 5 is turned into pseudo-particulate matter and ascending speed of atmospheric gas flow is lowered so that most of the produced dust is made to precipitate and load of a dust collector 6 is lowered.

Description

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

【0001】[0001]

【発明の属する技術分野】この発明は、経済性に優れる
焼結設備排鉱部の集塵方法に関し、特に焼結された高温
焼結鉱を破砕するときに生じる多量の粉塵の集塵方法を
提案するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of collecting dust from a sintering equipment ore, which is excellent in economical efficiency, and more particularly to a method of collecting a large amount of dust generated when crushing a sintered high-temperature sinter. It is a suggestion.

【0002】一般に焼結設備では、給鉱部、配合槽、排
鉱部およびコンベアなどで発生する粉塵の集塵を、電気
集塵機等を用いて行っている。この集塵においては、給
鉱部、配合槽に比べ排鉱部での集塵負荷が大きい。すな
わち、排鉱部においては、焼結後の赤熱高温焼結鉱を破
砕機で破砕処理するため、焼結鉱の破砕時の排鉱部は、
発生粉塵量が上記各部位に比し非常に多く、また、発生
ガス量も多く高温雰囲気となって、その集塵負荷が過大
となる。
Generally, in a sintering facility, dust generated in a feeder, a mixing tank, a discharger, a conveyor, and the like is collected using an electric dust collector or the like. In this dust collection, the dust collection load is larger in the mining section than in the mining section and the mixing tank. In other words, in the mining section, since the red hot high-temperature sinter after sintering is crushed by a crusher, the mining section at the time of crushing the sinter is
The amount of generated dust is much larger than each of the above portions, and the amount of generated gas is also large, resulting in a high-temperature atmosphere, and the dust collection load becomes excessive.

【0003】そのため、焼結鉱の破砕時に集塵能力が不
足した際には、電気集塵後に排出される煙突から赤煙が
排出される、すなわち粉塵が大気中に排出されるという
問題があり、経済的なその解決方法が望まれている。
[0003] Therefore, when the dust collecting capacity is insufficient when sintering ore is crushed, there is a problem that red smoke is discharged from a chimney discharged after electric dust collection, that is, dust is discharged into the atmosphere. An economical solution is desired.

【0004】[0004]

【従来の技術】排鉱部の集塵技術については、例えば、
特開平7-151472号公報(焼結鉱の粉塵集塵方法)が提案
されており、破砕機の下方から圧縮空気を焼結鉱に噴射
させ、破砕時に発生した粉塵を強制的に浮上させて集塵
効果を向上させる方法が開示されている。この方法は、
排鉱部の粉塵を効率よく集塵部分に導びき集塵しようと
するものであるが、焼結鉱の破砕時に多量に発生する粉
塵の大気中への排出を防止するためには、多量に発生す
る粉塵量のピークに合せて集塵機の能力を増大させてお
く必要があり、その設備費が高騰し、経済性に劣るとい
う問題がある。
2. Description of the Related Art Regarding the dust collection technology of a mining section, for example,
Japanese Patent Application Laid-Open No. Hei 7-151472 (a method for collecting dust from sinter) has been proposed, in which compressed air is injected into the sinter from below the crusher to forcibly lift the dust generated during crushing. A method for improving the dust collecting effect is disclosed. This method
The dust from the mining section is efficiently guided to the dust collecting section to collect the dust.However, in order to prevent the large amount of dust generated during the crushing of the sintered ore into the atmosphere, a large amount of dust is required. It is necessary to increase the capacity of the dust collector according to the peak of the amount of generated dust, and there is a problem that the cost of the equipment is soared and the economic efficiency is poor.

【0005】[0005]

【発明が解決しようとする課題】この発明は、前記した
問題点を有利に解決しようとするものであり、排鉱部で
の焼結鉱の破砕時に多量に発生する粉塵の集塵機へ吸引
される粉塵量を減少させ、集塵機の能力を増大させるこ
となく、効果的かつ経済的な焼結設備排鉱部の集塵方法
を提案することを目的とする。
SUMMARY OF THE INVENTION The present invention advantageously solves the above-mentioned problems, and sucks a large amount of dust generated during crushing of a sintered ore in an ore-discharging section into a dust collector. An object of the present invention is to propose an effective and economical dust collection method for a sintering facility mining section without reducing the amount of dust and increasing the capacity of a dust collector.

【0006】[0006]

【課題を解決するための手段】発明者らは、焼結鉱の破
砕時に多量に発生する粉塵と高温ガスのピークを減少さ
せることを種々検討した結果、ミスト噴霧することが極
めて有効であることを知見し、この発明を達成したもの
である。すなわち、この発明の要旨とするところは以下
の通りである。
Means for Solving the Problems The inventors of the present invention have conducted various studies to reduce the peak of dust and high-temperature gas generated when sintering is crushed, and found that spraying mist is extremely effective. And found the present invention. That is, the gist of the present invention is as follows.

【0007】 焼結設備排鉱部で、焼結された高温の
焼結鉱を破砕機により破砕する際に発生する多量の粉塵
を、破砕機の上方に設けた集塵機で集塵するにあたり、
焼結鉱破砕時の粉塵の発生に合せて排鉱部にミスト噴霧
することを特徴とする焼結設備排鉱部の集塵方法(第1
発明)。
[0007] In the sintering equipment mining section, when a large amount of dust generated when the sintered high-temperature sintered ore is crushed by the crusher is collected by a dust collector provided above the crusher,
A dust collection method for a sintering facility exhaust part, characterized by spraying mist onto the exhaust part in accordance with the generation of dust during sinter crushing (No. 1)
invention).

【0008】 ミスト噴霧を、排鉱部の雰囲気温度が
設定値に達した時点で開始することを特徴とする第1発
明に記載の焼結設備排鉱部の集塵方法(第2発明)。
[0008] The dust collecting method for a sintering facility mining section according to the first invention, wherein the mist spraying is started when the atmospheric temperature of the mining section reaches a set value (second invention).

【0009】 ミスト粒径が、50〜200 μmの範囲で
ある第1発明または第2発明に記載の焼結設備排鉱部の
集塵方法(第3発明)。
[0009] The dust collection method for a sintering facility discharge section according to the first or second invention, wherein the mist particle size is in the range of 50 to 200 µm (third invention).

【0010】[0010]

【発明の実施の形態】この発明の作用効果について以下
に述べる。前記したように、焼結設備では、排鉱部での
集塵負荷が他の部位にくらべ多く、特に特定サイクルで
供給される赤熱高温焼結鉱の破砕時に多量の粉塵と高温
ガスとが発生し、この時に集塵機の負荷が過大となり、
大気中に粉塵が排出され問題となる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The function and effect of the present invention will be described below. As described above, in the sintering facility, the dust collection load in the mining part is larger than in other parts, and a large amount of dust and high-temperature gas are generated, especially when the red hot high-temperature sinter supplied in a specific cycle is crushed. At this time, the load of the dust collector becomes excessive,
Dust is emitted into the atmosphere, causing a problem.

【0011】そこで、この発明では焼結鉱破砕時の粉塵
の発生に合せて、排鉱部にミストを噴霧するようにする
ものである。
Therefore, according to the present invention, a mist is sprayed to a mined portion in accordance with the generation of dust at the time of sintering ore crushing.

【0012】すなわち、焼結鉱破砕時の粉塵と高温ガス
とが多量に発生している雰囲気中にミストを噴霧する
と、 雰囲気ガス温度が低下してそのボリュームが減少す
る。 雰囲気ガス温度が低下することで、雰囲気ガスの上
昇流速度が低下し、粉塵の多くが沈降し上方に設置され
ている集塵機に吸引される粉塵量が減少する。 粉塵が疑似粒子化することで集塵機に吸引される粉
塵量が減少する。 などの効果で、集塵機の負荷が軽減され、大気中への粉
塵の排出が防止できる。なお、疑似粒子化したりして沈
降した粉塵の多くは、破砕した焼結鉱に捕捉され、焼結
鉱の篩分け時に微粉として、あるいは焼結鉱に付着した
状態で高炉に装入され、鉄源として利用できる。
That is, when mist is sprayed into an atmosphere in which a large amount of dust and high-temperature gas are generated during sinter ore crushing, the temperature of the atmosphere gas is reduced and the volume thereof is reduced. As the ambient gas temperature decreases, the upward flow velocity of the ambient gas decreases, so that much of the dust settles down and the amount of dust sucked by the dust collector installed above decreases. The amount of dust sucked into the dust collector is reduced due to the pseudo-particle formation of the dust. Due to such effects, the load on the dust collector is reduced, and the discharge of dust to the atmosphere can be prevented. Much of the dust that has settled due to pseudo-particles is trapped by the crushed sinter, and is charged to the blast furnace as fine powder during sieving of the sinter or attached to the sinter, and Available as a source.

【0013】また、焼結鉱破砕時の粉塵の発生に合せる
ミスト噴霧の開始時期は、粉塵の発生とともに高温ガス
が発生して雰囲気温度が上昇するので、この雰囲気温度
を指標とし、この温度が特定値に達した時点でミスト噴
霧を開始することもよい。すなわち、排鉱部の雰囲気温
度を測定し、該雰囲気温度が設定値に達した時点を開始
時点とすれば良い。ここで、雰囲気温度の設定値は集塵
機能力に応じて定めれば良く、例えば、排鉱部で焼結鉱
の破砕時に多量に発生する高温の粉塵・ガス量と集塵機
の集塵・風量能力とを比較し、発生する粉塵・ガス量が
集塵・風量能力を超える量だけ、ミスト噴霧により雰囲
気温度の低下それにともなうガスボリュームの減量をし
てやればよく、この減量したガスボリュームに相当する
温度を上限として雰囲気温度を設定し、雰囲気温度がこ
の設定値に達した時点でミスト噴霧を開始すればよい。
一方、焼結鉱の排鉱部での落下サイクルに合わせて、こ
の落下タイミングで破砕機による破砕が行われ、この時
に粉塵の発生とともに高温ガスが発生し、雰囲気温度が
上昇する。したがってこの落下タイミングに合せてミス
ト噴霧を行い粉塵の疑似粒子化並びに雰囲気温度の低下
を行うこともよい。
[0013] In addition, the start time of the mist spraying in accordance with the generation of dust during sinter ore crushing, since high-temperature gas is generated along with the generation of dust and the ambient temperature rises, the ambient temperature is used as an index. It is also possible to start mist spraying when the specific value is reached. That is, the atmosphere temperature of the mining section is measured, and the time when the atmosphere temperature reaches the set value may be set as the start time. Here, the set value of the ambient temperature may be determined according to the dust collecting function, for example, the amount of high-temperature dust and gas generated in large quantities when sintering ore is crushed in the mining part, and the dust collecting and air volume capability of the dust collector. If the amount of dust and gas generated exceeds the dust collection and air flow capacity, the mist spray can be used to reduce the gas volume associated with the decrease in ambient temperature, and the upper limit of the temperature corresponding to this reduced gas volume The mist spraying may be started when the ambient temperature reaches this set value.
On the other hand, crushing is performed by a crusher at this falling timing in accordance with the falling cycle of the sinter in the mining section, and at this time, high temperature gas is generated along with generation of dust, and the ambient temperature rises. Therefore, it is also possible to perform mist spraying in accordance with the falling timing to make pseudo particles of dust and to lower the ambient temperature.

【0014】また、噴霧するミスト粒径は、雰囲気ガス
の冷却効果等の観点から小さい方が好ましいが、コスト
面から50μm以上とすることがよく、粒径が200 μm以
下であれば雰囲気ガスの冷却ができることから、ミスト
粒径は、50μm以上、200 μm以下とする。
The particle size of the mist to be sprayed is preferably small from the viewpoint of the cooling effect of the atmosphere gas and the like, but is preferably 50 μm or more from the viewpoint of cost. Since cooling can be performed, the mist particle size is set to 50 μm or more and 200 μm or less.

【0015】[0015]

【実施例】【Example】

実施例1 図1に焼結設備排鉱部の説明図を示す。図において、焼
結設備の排鉱部では、焼結直後の焼結鉱1は、赤熱状態
でパレット2により搬送され、パレット2とほぼ同じ大
きさの塊状で落下し、破砕機3により破砕される。この
破砕された焼結鉱はクーラ4へ運ばれ2次破砕されて製
品となる。
Example 1 FIG. 1 is an explanatory view of a sintering equipment discharge section. In the figure, in the mining section of the sintering equipment, the sintered ore 1 immediately after sintering is transported in a red-hot state by a pallet 2, falls in a lump having substantially the same size as the pallet 2, and is crushed by a crusher 3. You. The crushed sintered ore is conveyed to the cooler 4 and secondarily crushed into a product.

【0016】一方、この排鉱部では、焼結鉱1の破砕時
に粉塵が多量に発生するため、集塵フード5と集塵機
(電気集塵機)6とを設け、この集塵機6で排鉱部はも
とより、その他の給鉱部や配合槽等の集塵を全てまかな
うようになっている。
On the other hand, since a large amount of dust is generated at the time of crushing of the sintered ore 1, a dust collecting hood 5 and a dust collector (electric dust collector) 6 are provided in the mining section. And all other dust collection stations and compounding tanks.

【0017】そして、この排鉱部にはこの発明を実施す
るため、ミストを噴霧するミストノズル7および雰囲気
温度を測定する温度計8が設置されている。
In order to carry out the present invention, a mist nozzle 7 for spraying mist and a thermometer 8 for measuring an ambient temperature are installed in the mining section.

【0018】つぎに、この図1に示す設備を用いて行っ
た実施例を以下に述べる。1は焼結鉱であり、焼結鉱1
を搬送するパレット2が落下する塊状の焼結鉱1は破砕
機3で破砕される。この破砕により、多量の高温ガスと
粉塵が発生し雰囲気温度の上昇が始まる。この高温ガス
の発生により上昇する雰囲気温度を温度計8で検知し、
その温度が500 ℃になった時点でミストノズル7から粒
径:200 μmのミストを噴霧量:8t/h で噴霧した。本
例ではミスト噴霧開始の雰囲気温度設定値を500 ℃、ミ
スト噴霧停止の雰囲気温度設定値を200 ℃とした。
Next, an embodiment performed using the equipment shown in FIG. 1 will be described below. Reference numeral 1 denotes a sintered ore, and a sintered ore 1
The sinter ore 1 in the form of a block on which the pallet 2 for transporting the sinter falls is crushed by the crusher 3. Due to this crushing, a large amount of high-temperature gas and dust are generated, and the atmospheric temperature starts to rise. The temperature of the atmosphere rising due to the generation of the high-temperature gas is detected by the thermometer 8,
When the temperature reached 500 ° C., a mist having a particle size of 200 μm was sprayed from the mist nozzle 7 at a spray amount of 8 t / h. In this example, the set ambient temperature at the start of mist spraying was 500 ° C., and the set ambient temperature at the stop of mist spraying was 200 ° C.

【0019】その結果、当然のことながら雰囲気温度が
500 ℃から200 ℃に低下し、そのガスボリュームは40%
減少した。そして、これまで集塵フード5で吸引されて
いた多量に発生した粉塵は疑似粒子化され、雰囲気ガス
温度の低下とそれにともなうガスボリュームの減量によ
る雰囲気ガス上昇流速の低下とあいまって、発生した粉
塵の多くは沈降して集塵機の負荷が減少したため、煙突
から排気される粉塵は皆無であった。
As a result, naturally, the ambient temperature
Reduced from 500 ℃ to 200 ℃, the gas volume is 40%
Diminished. The large amount of dust that has been sucked up by the dust collecting hood 5 is converted into pseudo particles, and the generated dust is combined with the decrease in the ambient gas temperature and the accompanying decrease in the gas flow rate due to the decrease in the gas volume. Most of the dust settled and the load on the dust collector was reduced, so that no dust was exhausted from the chimney.

【0020】実施例2 次にこの図1に示す設備を用いて行った他の実施例を以
下に述べる。焼結鉱1を搬送するパレット2の搬送速
度:2.5m/min、パレット長さ:1.5mとする焼結設備の排
鉱部の集塵である。この条件では、焼結鉱は落下サイク
ルが36秒/回となり、このサイクルで破砕機3で破砕さ
れていく。この破砕により多量の粉塵と高温ガスが発生
し雰囲気温度は高温となるが、その発生量は破砕開始か
ら10秒間程度がピークになる。すなわち、36秒毎に約10
秒間高温、高粉塵の状況となっている。この本発明にお
いては、焼結鉱の落下サイクルに合わせて、ミスト噴霧
を少なくとも10秒間程度行うことがよく、前記高温、高
粉塵状況下のみミスト噴霧する。焼結鉱1がパレット2
から落下し破砕機3に達する時点からミスト噴霧を開始
し、このミスト噴霧継続時間を12秒間として36秒周期で
繰返してミスト噴霧し集塵を行った。ミスト噴霧にはミ
スト粒径:100 μm、噴霧量:10t/h のミストノズルを
使用した。その結果、雰囲気温度の上昇は250 ℃にとど
まり、ガスボリュームの顕著な増加が抑制され、大気中
に排出される粉塵は皆無であった。
Embodiment 2 Next, another embodiment performed using the equipment shown in FIG. 1 will be described below. This is dust collection at the mine sintering section of the sintering facility where the pallet 2 for conveying the sinter 1 is transported at a speed of 2.5 m / min and the pallet length is 1.5 m. Under these conditions, the sinter has a falling cycle of 36 seconds / times, and is crushed by the crusher 3 in this cycle. A large amount of dust and high-temperature gas are generated by this crushing, and the ambient temperature becomes high. However, the amount of generation reaches a peak about 10 seconds from the start of crushing. That is, about 10 every 36 seconds
High temperature and high dust for a second. In the present invention, mist spraying is preferably performed for at least about 10 seconds in accordance with the falling cycle of the sintered ore, and mist spraying is performed only under the high temperature and high dust conditions. Sinter 1 is pallet 2
The mist spraying was started from the time when the mist sprayer dropped from the crusher 3 and reached the crusher 3, and the mist spraying was repeated at a cycle of 36 seconds with the mist spraying continuation time being 12 seconds to collect dust. A mist nozzle having a mist particle diameter of 100 μm and a spray amount of 10 t / h was used for mist spraying. As a result, the rise in the ambient temperature was limited to 250 ° C., the remarkable increase in the gas volume was suppressed, and no dust was discharged into the atmosphere.

【0021】なお、排鉱部の粉塵ガス量は、集塵機がま
かなう総量の約1/4 であるが、上記したように焼結鉱破
砕時のこの部分からの集塵風量の低減がなされ、十分な
効果が確認された。
The amount of dust gas discharged from the mining section is about 1/4 of the total amount provided by the dust collector, but as described above, the amount of dust collected from this section during crushing of the sintered ore is reduced. Effect was confirmed.

【0022】一方、ミスト噴霧による雰囲気ガス中の水
分増加により、排鉱部壁面での水分の結露が問題となる
が、水分増加は8%程度であってその結露温度は50℃前
後となるが、壁面鉄皮温度は70℃以上であるので問題と
なることはなかった。
On the other hand, the moisture in the atmospheric gas due to the mist spray increases water dew condensation on the wall of the ore-mining section. However, the water increase is about 8% and the dew temperature is about 50 ° C. On the other hand, since the wall steel temperature was 70 ° C. or more, there was no problem.

【0023】[0023]

【発明の効果】この発明は、焼結設備排鉱部で、焼結さ
れた高温の焼結鉱の破砕時にミストを噴霧するものであ
り、この発明によれば、焼結鉱破砕時に多量に発生する
粉塵と高温ガスによる集塵機の負荷を軽減し、経済的か
つ効果的に大気中への粉塵の排出を防止できる。
According to the present invention, mist is sprayed when sintering high-temperature sintered ore in the sintering equipment discharge section. According to the present invention, a large amount of mist is sprayed during sintering ore crushing. The load on the dust collector due to the generated dust and high-temperature gas can be reduced, and the dust can be prevented from being discharged into the atmosphere economically and effectively.

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

【図1】焼結設備排鉱部の説明図である。FIG. 1 is an explanatory view of a sintering facility discharge section.

【符号の説明】[Explanation of symbols]

1 焼結鉱 2 パレット 3 破砕機 4 クーラ 5 集塵フード 6 集塵機 7 ミストノズル 8 温度計 DESCRIPTION OF SYMBOLS 1 Sinter ore 2 Pallet 3 Crusher 4 Cooler 5 Dust collection hood 6 Dust collector 7 Mist nozzle 8 Thermometer

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 焼結設備排鉱部で、焼結された高温の焼
結鉱を破砕機により破砕する際に発生する多量の粉塵
を、集塵機で集塵するにあたり、 焼結鉱破砕時の粉塵の発生に合せて排鉱部にミスト噴霧
することを特徴とする焼結設備排鉱部の集塵方法。
1. A large amount of dust generated when a sintered high-temperature sinter is crushed by a crusher in a sintering facility ore discharging section, and when a dust collector collects a large amount of dust, A dust collection method for a sintering facility, wherein mist is sprayed to the mine in accordance with the generation of dust.
【請求項2】 ミスト噴霧を、排鉱部の雰囲気温度が設
定値に達した時点で開始することを特徴とする請求項1
に記載の焼結設備排鉱部の集塵方法。
2. The method according to claim 1, wherein the mist spraying is started when the ambient temperature of the mining section reaches a set value.
2. A dust collection method for a sintering facility mining section according to item 1.
【請求項3】 ミスト粒径が、50〜200 μmの範囲であ
る請求項1または2に記載の焼結設備排鉱部の集塵方
法。
3. The method of claim 1, wherein the mist particle size is in the range of 50 to 200 μm.
JP23368397A 1997-08-29 1997-08-29 Method of collecting dust in ore discharge part of sintering equipment Withdrawn JPH1172291A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23368397A JPH1172291A (en) 1997-08-29 1997-08-29 Method of collecting dust in ore discharge part of sintering equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23368397A JPH1172291A (en) 1997-08-29 1997-08-29 Method of collecting dust in ore discharge part of sintering equipment

Publications (1)

Publication Number Publication Date
JPH1172291A true JPH1172291A (en) 1999-03-16

Family

ID=16958912

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23368397A Withdrawn JPH1172291A (en) 1997-08-29 1997-08-29 Method of collecting dust in ore discharge part of sintering equipment

Country Status (1)

Country Link
JP (1) JPH1172291A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100543297B1 (en) * 2001-12-20 2006-01-20 주식회사 포스코 Apparatus for sprinkling of sintered ore
KR100544580B1 (en) * 2001-12-21 2006-01-24 주식회사 포스코 Apparatus for adding mist to the cooler of sintered ore
CN102527482A (en) * 2011-10-12 2012-07-04 邱富仁 Quartz high temperature melting lump waterpower spurting breaking device
KR101709205B1 (en) * 2015-09-11 2017-02-22 주식회사 포스코 Device for crushing compact iron
JP2020085303A (en) * 2018-11-21 2020-06-04 日本製鉄株式会社 Sintered ore cooling device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100543297B1 (en) * 2001-12-20 2006-01-20 주식회사 포스코 Apparatus for sprinkling of sintered ore
KR100544580B1 (en) * 2001-12-21 2006-01-24 주식회사 포스코 Apparatus for adding mist to the cooler of sintered ore
CN102527482A (en) * 2011-10-12 2012-07-04 邱富仁 Quartz high temperature melting lump waterpower spurting breaking device
KR101709205B1 (en) * 2015-09-11 2017-02-22 주식회사 포스코 Device for crushing compact iron
JP2020085303A (en) * 2018-11-21 2020-06-04 日本製鉄株式会社 Sintered ore cooling device

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