JP4077718B2 - Melt treatment facility in waste melting treatment - Google Patents

Melt treatment facility in waste melting treatment Download PDF

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Publication number
JP4077718B2
JP4077718B2 JP2002351698A JP2002351698A JP4077718B2 JP 4077718 B2 JP4077718 B2 JP 4077718B2 JP 2002351698 A JP2002351698 A JP 2002351698A JP 2002351698 A JP2002351698 A JP 2002351698A JP 4077718 B2 JP4077718 B2 JP 4077718B2
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Japan
Prior art keywords
water
slag
melt
granulated
pit
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JP2002351698A
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Japanese (ja)
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JP2004181361A (en
Inventor
一輝 川田
光正 戸高
政史 山田
隆男 松葉
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Nippon Steel Engineering Co Ltd
Nippon Steel Plant Designing Corp
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Nittetsu Plant Designing Corp
Nippon Steel Engineering Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、廃棄物溶融処理において、廃棄物溶融炉から出湯した溶融物を水砕化して処理する溶融物処理設備に関する。
【0002】
【従来の技術】
一般廃棄物あるいは産業廃棄物等の廃棄物の溶融処理では、例えば廃棄物をコークス、石灰石等の副原料とともに廃棄物溶融炉に装入し、廃棄物を溶融スラグとして取り出し、溶融スラグを水砕処理し、水砕スラグを製造している(特許文献1参照)。
【0003】
図3は従来の溶融物処理設備のレイアウトである。溶融炉1から出滓した溶融スラグを炉毎に設置されている水砕ピット2に流し込み水砕水で急冷して水砕する。水砕ピット2には、スラグを分散させて細分化することにより高品質のスラグを精製するために、水砕ノズル3から流速約3〜5m/sの表層流を形成し、そこに溶融物を落下させて水砕している。水砕されて水砕ピットの底に沈殿したスラグは、水砕ピットの底部に設けられたスクレーパーコンベア5により水砕ピット2から水切りされながら取り出される。水砕ピット2から排出されるスラグ中には、後工程設備の機器を損傷させるなどの悪影響を与える大塊が混入しているので、振動篩16で大塊を除去する。
【0004】
大塊が除去されたメタルが混在したままのスラグは、スラグバンカー17上部に設置された湿式磁選機9まで垂直コンベヤ18で磁選ホッパー19へ搬送され、磁選フィーダー20で切り出され、湿式磁選機9で磁選水を添加し、磁選して磁着物と非磁着物のスラグに選別し、スラリー状のスラグを水切りコンベア21で水切りし、スラグバンカー17に投入する。スラグバンカー17には多量の付着水を伴なったスラグが入るため、スラグバンカー17からダンプで切り出す場合には路上での漏水を防ぐために十分な水切りが必要であり、スラリー状のスラグの水を切るため、スラグバンカー下部の切り出しゲート部のシート部から十分時間をかけて水を排出する。排出した水は水受け樋22を経て排水処理される。
【0005】
【特許文献】
特開2000−288523号公報
【0006】
【発明が解決しようとする課題】
従来、溶融炉毎に水砕ピットを設置し、また、水砕ピットから排出されるスラグ中の、後工程設備に悪影響を与える大塊を除去する振動篩を設置する必要があるため、設備費および建設費が高くなっていた。
【0007】
従来、水砕ピットに沈殿した水砕スラグは水砕ピット中のコンベヤで水切りを行った後、メタル混在のまま製品バンカ上部に設置された湿式磁選機まで機械式コンベヤで搬送し、湿式磁選機で再び磁選水を添加し磁選されたスラリー状のスラグを再度水切りしていた。この場合高所にある磁選機までの水砕スラグ搬送に多数のコンベヤを設置することになり大きなスペース及び設備費が発生する問題があった。
【0008】
また、従来は、スラリー状のスラグの水を切るため、スクリューコンベヤ又はスクレーパーコンベヤ等の水切リコンベヤを用い、さらにスラグバンカーの切り出しゲート部のシート部から十分時間をかけて水を排出する必要があった。しかし、ゲートの密封性が高いと水が排出できず、逆にシート面に積極的に隙間を設けると、水と共にスラグが流出する問題があった。
【0009】
また、従来は、スラリー輸送及び磁選水循環を行うためにポンプを設置しているが、このスラリー水及び磁選水は多量のスラグ微粒子を含むため、スラリーポンプとして軸シール部に新水が必要である。この新水が系内水の増加を招き、オーバーフローする形で流出し排水処理が必要であった。
【0010】
そこで、本発明は、高品質な溶融スラグを精製でき、設備費及び建設費が廉価で、メンテナンスも少なくて済む廃棄物溶融処理における溶融物処理設備を提供するものである。
【0011】
【課題を解決するための手段】
本発明の溶融物処理設備は、数基の廃棄物溶融炉から溶融物を一基ずつ出湯して溶融物を水砕化させる一基の水砕ピットが設置され、水砕ピットには出湯して落下したスラグを細分化する表層流を形成する水砕ノズルを各廃棄物溶融炉に対してそれぞれ配置し、出湯中の廃棄物溶融炉に対する水砕ノズル以外の水砕ノズルが表層流の形成を妨げないように退避可能に設けられ、水砕ピットに配置された、水砕スラグを掻き集めて取り出すスクレーパーコンベアの搬出口近傍の底部に一定サイズ以上の大塊を分離するロストルが設けられていることを特徴とする。
【0012】
前記構成において、ロストルの上方には水砕スラグに散水する散水ノズルが設けられ、ロストルの下方にはロストルを通過した水を受け入れ、磁着物と非磁着物であるスラグとをスラリー状態で磁選する湿式磁選機が配置されてもよく、また、湿式磁選機で選別されたスラリー状態のスラグを製品バンカ上まで輸送する水中ポンプおよび配管を備えてもよく、また、製品バンカが水切り機能を有することもでき、さらに、湿式磁選後のスラリー排水を製品バンカで水切りした磁選水を、水砕水、磁選水、大塊分離用の散水として循環させる水中ポンプおよび配管を備えてもよい。
【0013】
【発明の実施の形態】
本発明は、複数の溶融炉毎に水砕ピットを設けることなく、1基の水砕ピットで共通化する。複数の溶融炉からの溶融物を、共通の水砕ピットで処理することにより、ピットの保有水量が増加し、出湯時の水温上昇が抑えられ、スラグの品質向上に有利となる。また、従来は、複数の水砕ピットから排出されるスラグの集合コンベヤが必要であったが、本発明では1基の水砕ピットなので、集合コンベヤが不要となる。
【0014】
高品質のスラグを精製するためには、水砕ノズルから流速約3〜5m/sの表層流を形成し、そこに溶融物を落下させる必要があるが、水砕ピットを共有化する場合、他炉用の水砕ノズルが表層流形成の障害となる。そこで、本発明では、この障害を排除して水砕ピット共用化を実現させるために、表層流形成の障害となる水砕ノズルを退避自在の構造にする。
【0015】
また、本発明では、水砕ピットからスラグを掻き揚げるコンベヤ底面の一部をロストル化することにより、掻き揚げ過程で一定サイズ以上の大塊を分離する。その結果、従来必要であった振動篩を省略することができる。
【0016】
また、本発明では、水砕ピット出口で湿式磁選機を直結し、磁選後のスラグをスラリー状態のままスラリーポンプで製品バンカまで配管移送するレイアウトとすることにより、移送設備が大幅に簡略化できる。また製品バンカでスラリーの水切りを行うことで、磁選後の水切り装置を省略できる。
【0017】
また、本発明では、水切りにより発生する排水を、水中ポンプを用いて水砕ピット及び湿式磁選に必要な磁選水として戻し再利用を行う。また、磁選水を水砕ピットに設置しているロストル上部より散水することで大塊分離効率を大幅に高めることができる。また、ポンプを水中ポンプとすることで、軸シール水が不要となり、また直接槽内に設置することで配管も簡略化され、配管の閉塞などを防ぐことができる。
【0018】
また、本発明では、バンカ排出ゲート部を袋状にし、下方は排出部を密閉する方式とし、かつ上方を開放しこの部分から水をオーバーフローさせて水切りを行うことで、スラグの流出を防ぎつつ容易に排水することができる。
【0019】
【実施例】
図1は本発明の溶融物処理設備のレイアウト、図2(a)は大塊を分離するロストルの平面図、(b)は側面図である。
【0020】
図1において、複数の溶融炉1に対して一基の水砕ピット2を設置して共通化する。水砕ピット2には、各溶融炉1に対して、落下したスラグを細分化する流速約3〜5m/sの表層流を形成する水砕ノズル3がそれぞれ配置されている。水砕ピット2を共有化する場合、他炉用の水砕ノズル2が表層流形成の障害となるので、図1の拡大図に示すように、表層流形成の障害となる水砕ノズル2をシリンダー4により回動させて退避可能にする。なお、水砕ピット2の水には、系内の水切りされた水を循環して使用する。
【0021】
水砕されて水砕ピット2の底に沈殿したスラグは、水砕ピットの底部に設けられたスクレーパーコンベア5のスクレーパー6でかき集めて搬送される。スラグ中には、後工程設備の機器に悪影響を与える大塊を除去するために、図2に示すように、水砕ピット2からスラグを掻き揚げるコンベヤ底面の一部にロストル7を設けて、一定サイズ以上の大塊を分離する。ロストル7の上方には散水ノズル8が設けられ、大塊分離効率を上げるために散水する。ロストル7を通過した水は、湿式磁選機9の磁選水として利用する。
【0022】
水砕ピット2の出口で湿式磁選機9を直結し、磁選後のスラグをスラリー状態でスラリー貯槽10に移し、スラリーのままでスラリーポンプ11により水切りバンカー12までスラリー移送する。
【0023】
水切りバンカ12で水切りされた水は、水受け樋13からバンカー排水槽14に貯められて、水中ポンプ15により水砕ピット2、ロストル7の散水と磁選水として循環させる。
【0024】
【発明の効果】
本発明によれば、高品質な溶融スラグを精製でき、設備費及び建設費が廉価で、メンテナンスも少なくて済む溶融物処理設備が得られる。
【図面の簡単な説明】
【図1】 本発明の溶融物処理設備のレイアウトである。
【図2】 (a)は大塊を分離するロストルの平面図、(b)は側面図である。
【図3】 従来の溶融物処理設備のレイアウトである。
【符号の説明】
1:溶融炉 2:水砕ピット 3:水砕ノズル 4:シリンダー 5:スクレーパーコンベア 6:スクレーパー 7:ロストル 8:散水ノズル 9:湿式磁選機 10:スラリー貯槽 11:スラリーポンプ 12:水切りバンカー 13:水受け樋 14:バンカー排水槽 15:水中ポンプ 16:振動篩 17:スラグバンカー 18:垂直コンベヤ 19:磁選ホッパー 20:磁選フィーダー 21:水切りコンベア 水受け樋
[0001]
BACKGROUND OF THE INVENTION
TECHNICAL FIELD The present invention relates to a melt treatment facility for treating a molten material discharged from a waste melting furnace by water granulation in waste melting treatment.
[0002]
[Prior art]
In the melting treatment of waste such as general waste or industrial waste, for example, the waste is charged into a waste melting furnace together with auxiliary materials such as coke and limestone, the waste is taken out as molten slag, and the molten slag is granulated. It is processed to produce granulated slag (see Patent Document 1).
[0003]
FIG. 3 is a layout of a conventional melt processing facility. The molten slag discharged from the melting furnace 1 is poured into a granulation pit 2 provided for each furnace, and rapidly cooled with granulated water and granulated. In the granulated pit 2, in order to refine high quality slag by dispersing and subdividing the slag, a surface layer flow having a flow rate of about 3 to 5 m / s is formed from the granulated nozzle 3 and the melt The water is dropped and crushed. The slag that has been granulated and settled on the bottom of the granulation pit is taken out from the granulation pit 2 by the scraper conveyor 5 provided at the bottom of the granulation pit. In the slag discharged from the granulated pit 2, large lumps that have an adverse effect such as damaging the equipment of the post-processing equipment are mixed, so the large lumps are removed by the vibrating sieve 16.
[0004]
The slag from which the metal from which the large lumps have been removed is mixed is conveyed to the magnetic separation hopper 19 by the vertical conveyor 18 to the wet magnetic separator 9 installed on the slag bunker 17, cut out by the magnetic separation feeder 20, and wet magnetic separator 9 The magnetically segregated water is added to the slag, and the slag is separated into magnetic and non-magnetized slags. The slurry-like slag is drained by the draining conveyor 21 and is put into the slag bunker 17. Since slag with a large amount of adhering water enters the slag bunker 17, it is necessary to drain enough water to prevent water leakage on the road when the slag bunker 17 is cut out with a dump. In order to cut, water is discharged from the seat part of the cutting gate part below the slag bunker over a sufficient amount of time. The discharged water is drained through a water receiver 22.
[0005]
[Patent Literature]
Japanese Patent Laid-Open No. 2000-288523
[Problems to be solved by the invention]
Conventionally, it is necessary to install a granulation pit for each melting furnace, and to install a vibrating screen that removes large lumps in the slag discharged from the granulation pit that adversely affect post-processing equipment. And construction costs were high.
[0007]
Conventionally, the granulated slag that settled in the granulation pit is drained by the conveyor in the granulation pit, and then transported by a mechanical conveyor to the wet magnetic separator installed on the top of the product bunker with the metal mixed. Then, magnetically selected water was added again, and the slurry-like slag magnetically selected was drained again. In this case, a large number of conveyors are installed for conveying the granulated slag to the magnetic separator at a high place, and there is a problem that a large space and equipment costs are generated.
[0008]
Conventionally, in order to drain the slurry-like slag water, it has been necessary to use a drainage conveyor such as a screw conveyor or a scraper conveyor, and to drain the water from the sheet portion of the slag bunker's cutting gate portion over a sufficient amount of time. It was. However, if the sealing performance of the gate is high, water cannot be discharged. Conversely, if a gap is positively provided on the seat surface, there is a problem that slag flows out together with water.
[0009]
Conventionally, a pump is installed to perform slurry transportation and magnetic separation water circulation. However, since this slurry water and magnetic separation water contain a large amount of slag fine particles, new water is required for the shaft seal portion as a slurry pump. . This new water caused an increase in the system water, and it overflowed and needed to be treated.
[0010]
Therefore, the present invention provides a melt processing facility in waste melting processing that can purify high-quality molten slag, has low equipment costs and construction costs, and requires less maintenance.
[0011]
[Means for Solving the Problems]
The melt treatment facility of the present invention is provided with one granulation pit for discharging the melt one by one from several waste melting furnaces to granulate the melt, and the water granulation pit has a tapping water. A granulation nozzle that forms a surface flow that subdivides the slag that has fallen is arranged for each waste melting furnace, and a granulation nozzle other than the granulation nozzle for the waste melting furnace in the hot water forms a surface flow. A rooster that separates large blocks of a certain size or more is provided at the bottom near the exit of the scraper conveyor, which is disposed in the granulation pit and scrapes and collects the granulated slag. It is characterized by that.
[0012]
In the above configuration, a watering nozzle for sprinkling the granulated slag is provided above the rooster, and the water that has passed through the rooster is received below the rooster, and magnetically segregated magnetic material and non-magnetized slag in a slurry state. A wet magnetic separator may be arranged, and it may be equipped with a submersible pump and piping for transporting the slurry slag selected by the wet magnetic separator onto the product bunker, and the product bunker has a draining function Furthermore, a submersible pump and a pipe for circulating magnetically separated water obtained by draining slurry wastewater after wet magnetic separation with a product bunker as water for granulated water, magnetically separated water, and large mass separation may be provided.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, a single granulated pit is used in common without providing a granulated pit for each of the plurality of melting furnaces. By processing the melts from a plurality of melting furnaces in a common granulated pit, the amount of water held in the pit is increased, the rise in the water temperature during tapping is suppressed, and this is advantageous for improving the quality of the slag. Further, conventionally, a collective conveyor for slag discharged from a plurality of granulated pits is required. However, in the present invention, since a single granulated pit is used, no collective conveyor is required.
[0014]
In order to refine high-quality slag, it is necessary to form a surface layer flow with a flow velocity of about 3 to 5 m / s from the water granulation nozzle and drop the melt there, but when the water granulation pit is shared, The water granulation nozzle for other furnaces becomes an obstacle to the formation of the surface layer flow. Therefore, in the present invention, in order to eliminate this obstacle and realize the common use of the water granulation pit, the water granulation nozzle, which becomes an obstacle to the formation of the surface layer flow, is configured to be retractable.
[0015]
Further, in the present invention, a lump of a certain size or more is separated in the lifting process by converting a part of the bottom surface of the conveyor that lifts the slag from the granulated pit into a rooster. As a result, it is possible to omit the vibration sieve that has been conventionally required.
[0016]
Also, in the present invention, the transfer equipment can be greatly simplified by directly connecting the wet magnetic separator at the outlet of the granulated pit and by transferring the slag after magnetic separation to the product bunker with the slurry pump while in the slurry state. . Moreover, the draining device after magnetic separation can be omitted by draining the slurry with the product bunker.
[0017]
Moreover, in this invention, the waste_water | drain produced | generated by draining is returned and reused as a magnetic separation water required for a granulation pit and wet magnetic separation using an underwater pump. In addition, the mass separation efficiency can be greatly increased by spraying magnetically selected water from the upper part of the rooster installed in the granulation pit. Further, by using a submersible pump as the pump, shaft seal water is not necessary, and by installing it directly in the tank, the piping can be simplified and the blockage of the piping can be prevented.
[0018]
Further, in the present invention, the bunker discharge gate portion is formed in a bag shape, the lower portion is sealed, and the upper portion is opened and water is overflowed from this portion to drain water, thereby preventing slag from flowing out. It can be easily drained.
[0019]
【Example】
FIG. 1 is a layout of a melt processing facility of the present invention, FIG. 2 (a) is a plan view of a rooster that separates a large block, and (b) is a side view.
[0020]
In FIG. 1, a single granulated pit 2 is installed and shared for a plurality of melting furnaces 1. In the granulation pits 2, for each melting furnace 1, a granulation nozzle 3 for forming a surface layer flow having a flow velocity of about 3 to 5 m / s for subdividing the dropped slag is arranged. When the water granulation pit 2 is shared, the water granulation nozzle 2 for other furnaces becomes an obstacle to the formation of the surface layer flow. Therefore, as shown in the enlarged view of FIG. The cylinder 4 is rotated to be retractable. In addition, the water drained in the system is circulated and used as the water in the granulated pit 2.
[0021]
The slag that has been granulated and settled on the bottom of the granulated pit 2 is collected and conveyed by a scraper 6 of a scraper conveyor 5 provided at the bottom of the granulated pit. In order to remove large lumps that adversely affect the equipment of the post-process equipment in the slag, as shown in FIG. 2, a rooster 7 is provided on a part of the conveyor bottom surface where the slag is lifted from the granulated pit 2, Separate large lumps over a certain size. A watering nozzle 8 is provided above the rooster 7 and sprinkles water to increase the mass separation efficiency. The water that has passed through the rooster 7 is used as magnetically selected water of the wet magnetic separator 9.
[0022]
The wet magnetic separator 9 is directly connected at the outlet of the granulated pit 2, and the slag after magnetic separation is transferred to the slurry storage tank 10 in a slurry state, and the slurry is transferred to the draining bunker 12 by the slurry pump 11 while remaining in the slurry.
[0023]
The water drained by the draining bunker 12 is stored in the bunker drainage tank 14 from the water receiving tank 13 and is circulated by the submersible pump 15 as watering of the granulated pit 2 and rooster 7 and magnetically selected water.
[0024]
【The invention's effect】
ADVANTAGE OF THE INVENTION According to this invention, the melt processing equipment which can refine | purify a high quality molten slag, is cheap in equipment cost and construction cost, and requires little maintenance is obtained.
[Brief description of the drawings]
FIG. 1 is a layout of a melt processing facility of the present invention.
FIG. 2A is a plan view of a rooster that separates a large block, and FIG. 2B is a side view.
FIG. 3 is a layout of a conventional melt processing facility.
[Explanation of symbols]
1: Melting furnace 2: Granulation pit 3: Granulation nozzle 4: Cylinder 5: Scraper conveyor 6: Scraper 7: Rooster 8: Sprinkling nozzle 9: Wet magnetic separator 10: Slurry storage tank 11: Slurry pump 12: Draining bunker 13: Water catcher 14: Bunker drainage tank 15: Submersible pump 16: Vibrating sieve 17: Slag bunker 18: Vertical conveyor 19: Magnetic separation hopper 20: Magnetic separation feeder 21: Draining conveyor Water catcher

Claims (5)

数基の廃棄物溶融炉から溶融物を一基ずつ出湯して溶融物を水砕化させる一基の水砕ピットが設置され、水砕ピットには出湯して落下したスラグを細分化する表層流を形成する水砕ノズルを各廃棄物溶融炉に対してそれぞれ配置し、出湯中の廃棄物溶融炉に対する水砕ノズル以外の水砕ノズルが表層流の形成を妨げないように退避可能に設けられ、水砕ピットに配置された、水砕スラグを掻き集めて取り出すスクレーパーコンベアの搬出口近傍の底部に一定サイズ以上の大塊を分離するロストルが設けられていることを特徴とする溶融物処理設備。One granulation pit is installed to discharge the melt from several waste melting furnaces one by one to granulate the melt, and the surface layer that subdivides the slag that falls out and falls in the granulation pit A water-split nozzle that forms a flow is arranged for each waste melting furnace, and a water-spraying nozzle other than the water sprinkling nozzle for the waste melting furnace in the tapping bath is provided so that it can be retracted so as not to prevent the formation of a surface flow. A melt processing facility characterized in that a roastol for separating a large block of a certain size or more is provided at the bottom in the vicinity of the exit of the scraper conveyor, which is disposed in the granulation pit and scrapes and collects the granulated slag. . ロストルの上方には水砕スラグに散水する散水ノズルが設けられ、ロストルの下方にはロストルを通過した水を受け入れ、磁着物と非磁着物であるスラグとをスラリー状態で磁選する湿式磁選機が配置されていることを特徴とする請求項1記載の溶融物処理設備。A water spray nozzle that sprinkles the granulated slag is provided above the rooster, and a wet magnetic separator that accepts the water that has passed through the rooster below the rooster and magnetically separates the magnetic and non-magnetic slag in a slurry state. The melt processing facility according to claim 1, wherein the melt processing facility is arranged. 湿式磁選機で選別されたスラリー状態のスラグを製品バンカ上まで輸送する水中ポンプおよび配管を備えたことを特徴とする請求項2記載の溶融物処理設備。The melt processing facility according to claim 2, further comprising a submersible pump and a pipe for transporting the slag in a slurry state selected by a wet magnetic separator to a product bunker. 製品バンカが水切り機能を有することを特徴とする請求項3記載の溶融物処理設備。The melt treatment facility according to claim 3, wherein the product bunker has a draining function. 湿式磁選後のスラリー排水を製品バンカで水切りした磁選水を、水砕水、磁選水、大塊分離用の散水として循環させる水中ポンプおよび配管を備えた請求項1〜4のいずれか1項に記載の溶融物処理設備。In any one of Claims 1-4 provided with the submersible pump and piping which circulate as the sprinkling water for granulated water, magnetic separation water, and a large lump separation of the magnetic separation water which drained the slurry waste water after wet magnetic separation with the product bunker. The melt treatment facility described.
JP2002351698A 2002-12-03 2002-12-03 Melt treatment facility in waste melting treatment Expired - Fee Related JP4077718B2 (en)

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JP4909101B2 (en) * 2007-01-24 2012-04-04 新日鉄エンジニアリング株式会社 Method and equipment for treating granulated material in waste melting furnace
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JP5725791B2 (en) * 2010-10-20 2015-05-27 三菱重工業株式会社 Slag discharge system and method of operating slag discharge system
JP5535868B2 (en) * 2010-10-20 2014-07-02 三菱重工業株式会社 Slag discharge system and method of operating slag discharge system
JP5601689B2 (en) * 2011-03-01 2014-10-08 新日鉄住金エンジニアリング株式会社 Slag treatment equipment in waste melting treatment equipment
CN104457084B (en) * 2014-12-25 2017-01-25 山东钢铁股份有限公司 Rapid cooling method for high-temperature materials
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