JPS589945A - Water-cooled breaker and removing method for oil-can from flash smelting furnace - Google Patents
Water-cooled breaker and removing method for oil-can from flash smelting furnaceInfo
- Publication number
- JPS589945A JPS589945A JP10734481A JP10734481A JPS589945A JP S589945 A JPS589945 A JP S589945A JP 10734481 A JP10734481 A JP 10734481A JP 10734481 A JP10734481 A JP 10734481A JP S589945 A JPS589945 A JP S589945A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- furnace
- breaker
- flash
- cans
- 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.)
- Pending
Links
- 238000003723 Smelting Methods 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 title claims description 12
- 239000000498 cooling water Substances 0.000 claims description 11
- 238000002844 melting Methods 0.000 claims description 10
- 210000002105 tongue Anatomy 0.000 claims 2
- 239000007789 gas Substances 0.000 abstract description 12
- 239000000295 fuel oil Substances 0.000 abstract description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052802 copper Inorganic materials 0.000 abstract description 5
- 239000010949 copper Substances 0.000 abstract description 5
- 239000000428 dust Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 238000009825 accumulation Methods 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 230000035699 permeability Effects 0.000 abstract 1
- 239000002912 waste gas Substances 0.000 abstract 1
- 238000003780 insertion Methods 0.000 description 7
- 230000037431 insertion Effects 0.000 description 7
- 230000008018 melting Effects 0.000 description 6
- 238000012546 transfer Methods 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 241000282326 Felis catus Species 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、自溶製練で使用する自溶炉のアップティ)部
に堆積したベコを除去する尋に使用するための水冷式ブ
レーカ−及び盤ベコを除去する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a water-cooled breaker for use in removing debris accumulated in the up-tee portion of a flash furnace used in flash smelting, and a method for removing debris from the plate. Regarding.
一般忙、銅鉱石の溶錬に用いられる自溶炉で発生する排
ガスは、その1覆が1.300℃と非常忙高く、しかも
この排ガス中には液体状の鉱石であるダストが多く含ま
れている。この排ガスは自溶炉の先に取付けられたがイ
ラによって排熱の1収が行われ冷却される。従って、自
溶炉の排ガス出口であるアップティクを上記?イラ七の
継ぎ部において、排ガスが冷却されてslf勾配が非常
忙大きくなり%また冷却された上記ダストは半一体化し
て継ぎ部に堆積する。この堆積したものは、通常自溶製
錬のベコと呼ばれ、ベコの堆積が成長する2自溶炉排ガ
スの通気抵抗が増加し、ついには通気不能となる。The exhaust gas generated in the flash smelting furnace used for smelting copper ore is extremely high at 1.300°C, and moreover, this exhaust gas contains a lot of dust, which is liquid ore. ing. This exhaust gas was installed at the tip of the flash furnace, and the exhaust heat was collected and cooled by the furnace. Therefore, is the uptick, which is the exhaust gas outlet of the flash furnace, mentioned above? At the joint, the exhaust gas is cooled and the SLF gradient becomes very large.The cooled dust becomes semi-integrated and deposits at the joint. This deposit is usually called a flash smelting smelter, and the ventilation resistance of the two flash smelting furnace exhaust gases in which the deposit grows increases, eventually making it impossible to vent.
従来の上記ベコの除去方法の例として、アラブチ4り部
で重油を1!いベコをflI解除未除去方法が知られて
いるが、これKは次の欠点がある。第1に、ベコを溶解
するKはアップティクを通過する#ガスのil@1.3
00℃より本高くしなければならないだ妙でなく、ベコ
の熱が一イラーを通じて逃けることも考慮しなければな
らない、従って、ベコの溶解効率は悪く、重油の消費量
4多大となる。第2に、重油の便用により排ガスが増加
し、その結果がイラーの熱負荷が増大し、また、自溶炉
排熱−イラー特有のダスト付着(よるがイラーの熱回収
率が低下すゐ。第3に、アップティクの天井及び側壁の
構造は煉瓦あるいはキャスタブル耐火物となっているが
、長期の重油使用により煉瓦及びキャスタデル耐火物の
損耗が著しくなり、がイラーの放散熱損失が多くなる、
第4に、自溶炉のセラトラ−は銅鉱石の溶解及び化学反
応によってで11九皺、鏝を分離しているが、竜ットラ
ーから鏝を流出させるときにアップティクからの重油燃
焼による溶融又は牛溶触状態のベコが優と混合し、これ
が鏝の抜口につまる郷の障害をも九らす。As an example of the conventional method for removing the above-mentioned beko, heavy oil is poured into the 4-barrelation section. A method of unremoval of flI is known, but this method has the following drawbacks. First, the K that dissolves Beko is the # gas il @ 1.3 that passes through the uptick.
Not only does it have to be heated to a temperature higher than 00°C, but it must also be taken into consideration that the heat of the beco will escape through the iller.Therefore, the dissolution efficiency of the beco is poor and the amount of heavy oil consumed will be large. Second, the use of heavy oil increases exhaust gas, which increases the heat load on the furnace, and also reduces the heat recovery rate of the furnace due to dust adhesion that is characteristic of flash furnace waste heat and furnaces. Thirdly, the ceiling and side walls of the uptick are made of brick or castable refractories, but long-term use of heavy oil causes significant wear and tear on the bricks and caster refractories, resulting in a large amount of heat loss due to heat dissipation from the wall. ,
Fourthly, the ceratora of a flash smelting furnace separates the 119 wrinkles and trowels by melting copper ore and chemical reactions, but when the trowel is discharged from the ryuttler, it melts or melts due to the burning of heavy oil from the uptick. Beko, who is in a molten state, mixes with Yuu, and this alleviates Go's trouble of getting stuck in the trowel's opening.
従来のベコの除去方法の他の例として、ダイナ!イトに
よってベコを破壊して除去する方法が知られている。こ
の方法は、炉を休止して行わなければならず非生産的で
あや、また、作業員、設備の安全の面からも問題が多い
、さら(ダイナiイトの扱いにけ特別の技術・熟練を要
し人件費−相当多くなる。Another example of traditional beko removal methods is Dyna! There is a known method of destroying and removing beko by using light. This method requires the furnace to be shut down, which is unproductive, and also poses many safety problems for workers and equipment. The labor cost will be considerably high.
本発明は、上記従来の欠点を幣消した自溶炉等に使用す
る水冷式ブレーカ−及び自溶炉ベコ除去方法を提供する
ことを目的とする本のであって、その構成上の特徴とす
るところは、ブレーカーにおいて、自溶炉内で高温ベコ
Ill央き尚てるブレーカ−のロッド部材の内部に循環
流路を設け″、該循環流路に冷却水を流すことである。The present invention is a book aimed at providing a water-cooled breaker for use in a flash furnace, etc., which eliminates the above-mentioned drawbacks of the conventional art, and a method for removing flash furnace cracks. However, in the breaker, a circulation flow path is provided inside the rod member of the breaker which heats up the high temperature inside the flash furnace, and cooling water is allowed to flow through the circulation flow path.
さら(、操業中の自溶炉内KtlPいて、ロッド部材の
内部に設けた循環流路に冷却水を流しながら、該ロッド
部材によってベコを除去すゐことを特徴とする自溶炉ベ
コ除去方法である。Furthermore, a method for removing slag in a flash melting furnace, which comprises removing sludge using a rod member while flowing cooling water through a circulation channel provided inside the rod member in the flash smelting furnace during operation. It is.
本発明は上記のようKII成されるから、重油をまった
く使用せず資―節約に貢献する。鵞た、自溶炉操業中に
シいても、炉内を負圧にして、炉の天井からベコを容易
に除去することができ、生産性の高いものである。ざら
に1本発IIAVcよるベコの除去は、害鳥で熟練を要
せず、人手も少なくてよい、すなわち、本発明は、従来
、ブレーカーロッドを自溶炉内に挿入すると数分のうち
に赤熱してし重イ、操粱中の自溶炉内でのブレーカ−ロ
ッドの使用は不可能であるという壱業者の常識を覆す一
期的なものである。Since the present invention is constructed using KII as described above, heavy oil is not used at all, contributing to resource savings. Even if the flash smelting furnace breaks down during operation, it can easily remove the debris from the ceiling of the furnace by creating a negative pressure inside the furnace, resulting in high productivity. Removal of beko with a single shot of IIAVc is a harmful bird and does not require skill and requires less manpower.In other words, the present invention conventionally eliminates the red heat within a few minutes when a breaker rod is inserted into a flash furnace. This is a one-time project that overturns the conventional wisdom among manufacturers that it is impossible to use a breaker rod in a flash smelting furnace during heavy operation.
以下・本発明の実糟例をaKついて説明する。Below, an actual example of the present invention will be explained with reference to aK.
本l@明による型槽炉用ブレーカ−1は、第111に示
すように、自溶炉の排ガス出口であるアップティク2と
がイラ4との継ぎ部の近傍に設けられたプレーカー挿入
口6から、アップティクI12に挿入される。ブレーカ
−1位、台車8Km付けられりf L/−カー操作装置
10によって保持されている0台車$は所定のレール上
を駆動装置12によって移動させられる。プレーカー操
作装置1,011、第1油圧シリンダー14、第2油圧
シリンダー゛16、支柱IHt18及び第5油圧シリy
l−3!0から構成される。第1油圧シリンダー14は
ブレーカー1を水平方向tc11勤するためのものであ
り。As shown in No. 111, the breaker 1 for mold tank furnaces by Book 1@Akira has a breaker insertion port provided near the joint between the uptick 2, which is the exhaust gas outlet of the flash smelting furnace, and the slug 4. 6, it is inserted into uptick I12. The breaker #1, a bogie 8 km attached, and a f L/-0 bogie $ held by a car operating device 10 are moved by a drive device 12 on a predetermined rail. Play car operating device 1,011, first hydraulic cylinder 14, second hydraulic cylinder 16, column IHt18 and fifth hydraulic cylinder y
Consists of l-3!0. The first hydraulic cylinder 14 is for operating the breaker 1 in the horizontal direction tc11.
fIX2t/に圧シリンダ−16はブレーカー1を支柱
部材180下端を中心e11転させるためのものであり
、第3油圧シリンダー20はプレーカー挿入口コ21に
崗けて前後に移動させるためのものである。ブレーカー
1は、112図に示すように、空気圧シリンダー22、
ロッド部材24、ロッrs材24に取付けられた給水管
1!6及び排水管!8によって構成される。空気圧シリ
ンダー22は、4ないし5 kg/an’の空気圧によ
ってロッド部材24忙ベコ21の方向のへンマー力を加
えるためのものである。ロッド部材24の第1実権例は
、第2図に示すように、ロッド部材24の内11に2本
O円個孔30を設け、また先端部には一方の円筒孔30
から他方の円筒孔30に連絡させるための横断円筒孔3
zを設け、こo両端34をIII!によ〕塩める。ジッ
ド部材24は加工技術の関係から数本のロツPを継ぎ合
せて構成してもよい。The pressure cylinder 16 is for rotating the breaker 1 around the lower end of the support member 180, and the third hydraulic cylinder 20 is for moving the breaker 1 back and forth over the breaker insertion port 21. be. As shown in FIG. 112, the breaker 1 includes a pneumatic cylinder 22,
The rod member 24, the water supply pipe 1!6 and the drain pipe attached to the rod member 24! Consisting of 8. The pneumatic cylinder 22 is for applying a hammering force in the direction of the rod member 24 to the heel 21 with an air pressure of 4 to 5 kg/an'. A first practical example of the rod member 24 is, as shown in FIG.
A transverse cylindrical hole 3 for communicating with the other cylindrical hole 30
z, and both ends 34 of this III! Add salt. The jid member 24 may be constructed by joining several rods P together due to processing technology.
ロッド部材24のj12m!III例は、菖墨図に示す
ように、丸棒−材27の外壁の長さ方向に偶数本数の円
筒半割s#(又は樋状部材)29を溶接付けしたもので
あゐ。ロッド部材24の先端部の冷却水通路は、第1爽
總例と同じく横断円筒孔により構成する。j12m of rod member 24! In Example III, as shown in the iris diagram, an even number of cylindrical halves S# (or gutter-like members) 29 are welded to the outer wall of the round bar 27 in the length direction. The cooling water passage at the tip of the rod member 24 is constituted by a transverse cylindrical hole as in the first refreshing example.
自溶炉2のブレーカ−挿入口6は、第4図に示すように
、自溶炉2の天上部のアップティク部40近くK、1I
lllI自在なIl[,42が配置されている。As shown in FIG. 4, the breaker insertion port 6 of the flash furnace 2 is located near the uptick portion 40 at the top of the flash furnace 2 K, 1I.
IllI flexible Il[, 42 are arranged.
次(,1紀構成の自溶炉用デレーカーの作動について説
明する。操業中の自溶炉内を公知の手段によ)負圧KL
、自溶炉がら842を取シはずしてブレーカ−挿入口6
を開にする6次に、駆動値f11!を作動させて台車8
を適所kII動して、固定する。絖いて、第1シリンダ
ー14、第2シリンダー16、第5シリンダー20をそ
れぞれ作動させて、■ラド部材24をプレーカー挿入口
6に挿入する。この際冷却水が給水管26がらロッド部
材24に供給され続け、排水管28から排′出され続け
る1以上でベコ除去の準備が完了する。ベコ除去作動は
、gsシリンダー20及び空気圧シリンダ22の作動に
よりロッド部材24にハンマー力を与えて行う。Next, we will explain the operation of the deraker for flash-smelting furnaces with primary configuration. Negative pressure KL
, remove the flash furnace shell 842 and insert the breaker insertion port 6.
6 Next, drive value f11! Activate the trolley 8
Move it to the appropriate place and fix it. Then, the first cylinder 14, the second cylinder 16, and the fifth cylinder 20 are operated, respectively, and the rad member 24 is inserted into the plaaker insertion port 6. At this time, the cooling water continues to be supplied to the rod member 24 through the water supply pipe 26, and continues to be discharged from the drain pipe 28. Preparation for removing the water is completed. The removal operation is performed by applying hammer force to the rod member 24 by operating the gs cylinder 20 and the pneumatic cylinder 22.
次に、冷却水によるロッド部材24の設計法及び冷却能
力を数値例を用いて説明する。一般に1銅製錬に使用さ
れる自溶炉のアップティクにおける熱伝達量は100
Mcal 7m2h K達する0例えば、ロッド部材2
4の直径100sa*、炉内に挿入されるロッド部材2
4の長さ4.0OOtgとすれば、ロッドに伝わる熱量
は126 、4Mcsl/hとなる。Next, the design method and cooling capacity of the rod member 24 using cooling water will be explained using numerical examples. Generally, the amount of heat transfer in the uptick of a flash smelting furnace used for copper smelting is 100
Mcal 7m2h K reaches 0 For example, rod member 2
4 diameter 100sa*, rod member 2 inserted into the furnace
If the length of rod 4 is 4.0OOtg, the amount of heat transferred to the rod will be 126, 4Mcsl/h.
冷却水が供給時20℃%排出時60℃を繍持するとすれ
ば、5 、2 t/h の冷却水を流すことが必要で
ある。iた、ロッド部材24の直径100fl。Assuming that the cooling water maintains a temperature of 20°C during supply and 60°C during discharge, it is necessary to flow 5.2 t/h of cooling water. The diameter of the rod member 24 is 100 fl.
ロッド部材24の円筒孔30の直径20m11.冷却水
からロッド部材240表面までの最大距離を50Uとし
、高fflガスの伝達熱量100 、000にcal
7m2h ℃s冷却水温[40℃とする。熱伝達に関す
る一般式は、
q=α(tb −ta) Kcal/ m2h ℃=λ
/ l (tc −tb)にcat/mht:で表わさ
れる。ここで、αは熱伝達率(Kcat/m2h ℃)
、λは熱伝導率(にcal / mh ’C)、tは厚
(m)である。従って、
100.000にcat/m2ht: = 2,000
にca4/m2ht:X (tb−40℃)ここで、ロ
ッド部材の冷却水に接する面の温度tbを90℃とする
と、
100.000 Kcat/m2h ℃ = 451
0.05にca4/mh℃X (to−9o℃tc =
201℃
すなわち、ロッド部材のガスに接する外面の温度は20
1℃となる。The diameter of the cylindrical hole 30 of the rod member 24 is 20 m11. The maximum distance from the cooling water to the surface of the rod member 240 is 50U, and the amount of heat transferred from the high ffl gas is 100,000 cal.
7m2h ℃s Cooling water temperature [40℃. The general formula for heat transfer is: q=α(tb -ta) Kcal/m2h ℃=λ
/ l (tc - tb) is expressed as cat/mht:. Here, α is the heat transfer coefficient (Kcat/m2h °C)
, λ is the thermal conductivity (in cal/mh'C), and t is the thickness (m). Therefore, 100.000 cat/m2ht: = 2,000
ca4/m2ht:
0.05 to ca4/mh℃X (to-9o℃tc =
201℃ In other words, the temperature of the outer surface of the rod member in contact with the gas is 20℃.
It becomes 1℃.
従って、該ロッド部材は炉内温度に充分耐えることがで
きる。Therefore, the rod member can sufficiently withstand the temperature inside the furnace.
次K、本発明を実際に大型自溶炉に使用した場合のアッ
グテイク通気抵抗、ベコ溶解の重油消費量及びベコ溶解
の電気消費量を、上記重油をたいてベコを溶解する場合
と比較して示す。上記ベコ溶解の電気消費は、自溶炉の
通風用ファンの駆動のためのものである。Next, when the present invention is actually used in a large flash furnace, the ventilation resistance of Agtake, the heavy oil consumption of Beko melting, and the electricity consumption of Beko melting will be compared with the case where heavy oil is used to melt Beko. show. The electricity consumption of the above-mentioned beco melting is for driving the ventilation fan of the flash melting furnace.
第1図は本発明の詳細な説明図、第2図はロッド部材の
第1実施例の横断面図、第3図はロッド部材の第2実施
例の縦断面図、第4図は自溶炉のグレーカー挿入部付近
の斜視図である。
1・・・自溶炉用ブレーカ−12・・・アップティク、
4・・・lイラ、6・・・ブレーカ−挿入口、8・・・
台車、10・・・プレーカー操作装置、24・・・ロッ
ド部材第4図Fig. 1 is a detailed explanatory diagram of the present invention, Fig. 2 is a cross-sectional view of the first embodiment of the rod member, Fig. 3 is a longitudinal sectional view of the second embodiment of the rod member, and Fig. 4 is a self-melting FIG. 3 is a perspective view of the vicinity of the gray car insertion part of the furnace. 1... Breaker for flash furnace - 12... Uptick,
4...Ira, 6...Breaker insertion port, 8...
Trolley, 10... Player operating device, 24... Rod member Fig. 4
Claims (1)
を設け、該循1IrItWsVc冷却水を流すことを特
徴とする(水冷式)ブレーカ− (8) 操業中の自溶炉において、ロッド部材の内部
に設けた循l1llfIt路に冷却水を流しながら、該
ロッド部材によってベコを除去すると2を4I徽とする
自溶炉ベロ除去方法。 +31 41許請求の範囲第2項において、上紀自熔炉
内を負圧KL、上配上記ド部材を上記自溶炉の天井部か
ら該炉内に挿入する自溶炉ベコ除去方法。[Scope of Claims] (1) A (water-cooled) breaker characterized in that a circulation flow path is provided in 11 of the rod members of the breaker, and the circulation 1IrItWsVc cooling water flows therethrough (8) Self-fusing during operation A method for removing tongues in a flash-smelting furnace, in which the tongues are removed by the rod member while flowing cooling water through a circulation passage provided inside the rod member in the furnace. +31 41. The flash-melting furnace removal method according to claim 2, wherein the inside of the flash-melting furnace is kept under negative pressure KL, and the upper member is inserted into the flash-melting furnace from the ceiling of the furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10734481A JPS589945A (en) | 1981-07-09 | 1981-07-09 | Water-cooled breaker and removing method for oil-can from flash smelting furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10734481A JPS589945A (en) | 1981-07-09 | 1981-07-09 | Water-cooled breaker and removing method for oil-can from flash smelting furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS589945A true JPS589945A (en) | 1983-01-20 |
Family
ID=14456665
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10734481A Pending JPS589945A (en) | 1981-07-09 | 1981-07-09 | Water-cooled breaker and removing method for oil-can from flash smelting furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS589945A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0483829A (en) * | 1990-07-25 | 1992-03-17 | Sumitomo Metal Mining Co Ltd | Operation of flash smelting furnace |
| WO2002001131A1 (en) * | 2000-06-29 | 2002-01-03 | Outokumpu Oyj | Apparatus for removing dust accretions from a smelting furnace |
| KR101089375B1 (en) | 2009-12-10 | 2011-12-02 | 엘에스니꼬동제련 주식회사 | Method and apparatus for preventing dust accumulation in bath smelting process |
| JP2012067372A (en) * | 2010-09-27 | 2012-04-05 | Pan Pacific Copper Co Ltd | Structure of lance inserting hole part |
| WO2013167810A1 (en) * | 2012-05-09 | 2013-11-14 | Outotec Oyj | Method and arrangement for removing outgrowth in a suspension smelting furnace |
-
1981
- 1981-07-09 JP JP10734481A patent/JPS589945A/en active Pending
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0483829A (en) * | 1990-07-25 | 1992-03-17 | Sumitomo Metal Mining Co Ltd | Operation of flash smelting furnace |
| WO2002001131A1 (en) * | 2000-06-29 | 2002-01-03 | Outokumpu Oyj | Apparatus for removing dust accretions from a smelting furnace |
| US6797229B2 (en) | 2000-06-29 | 2004-09-28 | Outokumpu Oyj | Apparatus for removing dust accretions from a smelting furnace |
| AP1489A (en) * | 2000-06-29 | 2005-11-30 | Outotec Oyj | Apparatus for removing dust accretions from a smelting furnace. |
| KR100763295B1 (en) | 2000-06-29 | 2007-10-04 | 오또꿈뿌 오와이제이 | Device for removing dust accumulation from the melting furnace |
| KR101089375B1 (en) | 2009-12-10 | 2011-12-02 | 엘에스니꼬동제련 주식회사 | Method and apparatus for preventing dust accumulation in bath smelting process |
| JP2012067372A (en) * | 2010-09-27 | 2012-04-05 | Pan Pacific Copper Co Ltd | Structure of lance inserting hole part |
| WO2013167810A1 (en) * | 2012-05-09 | 2013-11-14 | Outotec Oyj | Method and arrangement for removing outgrowth in a suspension smelting furnace |
| CN104321606A (en) * | 2012-05-09 | 2015-01-28 | 奥图泰(芬兰)公司 | Method and arrangement for removing outgrowth in a suspension smelting furnace |
| CN104321606B (en) * | 2012-05-09 | 2016-03-23 | 奥图泰(芬兰)公司 | For removing the method and apparatus of the accessory substance in suspension smelting furnace |
| EA026558B1 (en) * | 2012-05-09 | 2017-04-28 | Оутотек (Финлэнд) Ой | Method and arrangement for removing outgrowth in a suspension smelting furnace |
| US9845993B2 (en) | 2012-05-09 | 2017-12-19 | Outotec (Finland) Oy | Method and arrangement for removing outgrowth in a suspension smelting furnace |
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