JPH0443701Y2 - - Google Patents
Info
- Publication number
- JPH0443701Y2 JPH0443701Y2 JP8598688U JP8598688U JPH0443701Y2 JP H0443701 Y2 JPH0443701 Y2 JP H0443701Y2 JP 8598688 U JP8598688 U JP 8598688U JP 8598688 U JP8598688 U JP 8598688U JP H0443701 Y2 JPH0443701 Y2 JP H0443701Y2
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- concentrate
- burner
- pipe
- center
- 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
Links
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 54
- 229910052760 oxygen Inorganic materials 0.000 claims description 54
- 239000001301 oxygen Substances 0.000 claims description 54
- 239000012141 concentrate Substances 0.000 claims description 45
- 239000000446 fuel Substances 0.000 claims description 39
- 238000002347 injection Methods 0.000 claims description 37
- 239000007924 injection Substances 0.000 claims description 37
- 238000007664 blowing Methods 0.000 claims description 22
- 238000003723 Smelting Methods 0.000 description 31
- 238000006243 chemical reaction Methods 0.000 description 26
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 7
- 238000002844 melting Methods 0.000 description 7
- 239000002994 raw material Substances 0.000 description 5
- 239000010949 copper Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012768 molten material Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Nozzles For Spraying Of Liquid Fuel (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、自熔炉において製錬原料と反応用空
気とを吹込み熔錬反応を起させる精鉱バーナーに
関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a concentrate burner that causes a smelting reaction by blowing smelting raw materials and reaction air into an flash smelting furnace.
硫化精鉱を原料とする製錬炉の一つの自熔炉と
呼ばれる自熔製錬炉がある。
There is a self-melting smelting furnace called a flash smelting furnace, which is one type of smelting furnace that uses sulfide concentrate as a raw material.
第5図に示したように自熔製錬炉1は、頂部に
精鉱バーナー2が設けられた反応塔3と、反応塔
3の下部に一端が接続され、且つ側面に〓抜口4
〓抜口5が設けられたセトラー6と、セトラー6
の他端に接続された拝煙道7とから基本的に構成
されている。そして、これによる製錬工程は次の
ようである。まず、硫化精鉱、フラツクス、補助
燃料等の製錬原料8は予熱された反応用空気9と
共に精鉱バーナー2から炉の反応塔3内に吹込ま
れる。反応塔3内において、この製錬原料8の可
燃性成分である硫黄と鉄は高温の反応用空気9と
反応し、セトラー6に溜められる。この湯溜り部
であるセトラー6では熔体は比重差によつてCu2
SとFeSの混合物である〓10と、2FeO・SiO2
を主成分とする〓11分けられる。〓11は〓抜
口4から排出され、電気錬〓炉12に導入され
る。一方、〓10は〓抜口5から次の工程である
転炉の要求に応じて抜き出される。 As shown in FIG. 5, the flash smelting furnace 1 includes a reaction tower 3 equipped with a concentrate burner 2 at the top, one end connected to the lower part of the reaction tower 3, and an outlet 4 on the side.
〓Settler 6 with outlet 5 and settler 6
It basically consists of a flue 7 connected to the other end. The smelting process is as follows. First, smelting raw materials 8 such as sulfurized concentrate, flux, and auxiliary fuel are blown together with preheated reaction air 9 from the concentrate burner 2 into the reactor tower 3 of the furnace. In the reaction tower 3, sulfur and iron, which are combustible components of the smelting raw material 8, react with the high temperature reaction air 9 and are stored in the settler 6. In the settler 6, which is the hot water pool, the molten material is Cu 2 due to the difference in specific gravity.
〓10, which is a mixture of S and FeS, and 2FeO・SiO 2
The main component is divided into 11 parts. 11 is discharged from the outlet 4 and introduced into the electric smelting furnace 12. On the other hand, the material 10 is extracted from the outlet 5 in accordance with the requirements of the next process, the converter.
又、反応塔3内に発生する高温排ガス13はセ
トラー6及び排煙道7を通つて排熱ボイラー14
で冷却される。電気錬〓炉12に入つて〓は電極
15によつて通電された電熱によつて加熱保持さ
れ、必要によつて電気錬〓炉12に装入された塊
状鉱石や塊状フラツクス等と混合され銅分は更に
炉底に沈降し、僅かに残つた銅分を含んだ〓のみ
が抜き口16から炉外に排出される。 In addition, the high-temperature exhaust gas 13 generated in the reaction tower 3 passes through the settler 6 and the exhaust flue 7 to the exhaust heat boiler 14.
cooled down. After entering the electric smelting furnace 12, the copper is heated and maintained by electric heat applied by an electrode 15, and is mixed with lump ore, lump flux, etc. charged into the electric smelting furnace 12 as necessary. The copper content further settles to the bottom of the furnace, and only the remaining copper content is discharged from the furnace through the outlet 16.
このような自熔製錬炉においては、製錬原料が
反応塔内を落下する間に反応が完結することが必
要であり、完結しない場合には未反応物の一部は
排ガス13と共に排熱ボイラーの方へ持ち去られ
て煙灰となり、他の一部は反応塔3の下部の熔体
表面上に堆積して〓の生成を妨げるようになる。 In such a flash smelting furnace, it is necessary for the reaction to be completed while the smelting raw materials fall through the reaction tower, and if the reaction is not completed, some of the unreacted materials will be released as waste heat along with the exhaust gas 13. It is carried away to the boiler and becomes smoke ash, and the other part is deposited on the surface of the melt in the lower part of the reaction tower 3, which prevents the formation of smoke.
従つて、反応塔3内の精鉱の酸化反応が最も活
発で高温となる場所であるフオーカスの位置が、
適正な範囲で可能な限り上部になるようにするこ
とが操炉上重要である。 Therefore, the focus position where the oxidation reaction of the concentrate in the reaction tower 3 is most active and the temperature is
It is important for reactor operation that it be located as high as possible within an appropriate range.
ところで近年、自熔炉の熱バランスを改善し生
産性を高めるために、精鉱バーナーに酸素吹込み
管と補助燃料導入管とを組込んだ自熔製錬用精鉱
バーナーが使用されている。即ち、第4図の概略
断面図に示すように、下端にベンチユリー状の絞
り部が形成され、上部側面に反応用空気導入口1
7を有するバーナー本体18の中央にその先端が
絞り部よりやゝ下方に突出するように管状の精鉱
シユート19を垂設し、精鉱シユート19の中心
を貫通する酸素吹込み管20を設け、酸素吹込み
管20中を同心をなすように貫通して、酸素吹込
み管20の下端まで延長する補助燃料導入管21
を設けた自熔製錬用精鉱バーナーである。 Incidentally, in recent years, in order to improve the heat balance of the flash smelting furnace and increase productivity, a concentrate burner for flash smelting has been used in which an oxygen blowing pipe and an auxiliary fuel introduction pipe are incorporated into the concentrate burner. That is, as shown in the schematic cross-sectional view of FIG.
A tubular concentrate chute 19 is vertically disposed in the center of the burner body 18 having a burner body 18 with its tip protruding slightly below the constriction part, and an oxygen blowing pipe 20 is provided passing through the center of the concentrate chute 19. , an auxiliary fuel introduction pipe 21 that extends concentrically through the oxygen injection pipe 20 and extends to the lower end of the oxygen injection pipe 20;
This is a concentrate burner for self-melting smelting.
そしてこの種の自熔製錬用精鉱バーナーにおい
ては、酸素吹込み管20及び補助燃料導入管21
の下端に、中央に燃料噴出孔22を有し、燃料噴
出孔22を取り巻くように複数の酸素噴出孔23
を具えたバーナーチツプ24を接合して用いるの
が通常であり、酸素吹込み管20に供給される酸
素は酸素噴出孔23より噴射され、補助燃料導入
管21を経て燃料噴出孔22から噴射される重油
等の燃料及び精鉱シユート19から落下する精鉱
と反応するように構成されている。 In this type of self-smelting concentrate burner, an oxygen blowing pipe 20 and an auxiliary fuel introducing pipe 21
It has a fuel injection hole 22 in the center at the lower end, and a plurality of oxygen injection holes 23 surrounding the fuel injection hole 22.
It is normal to use a burner chip 24 equipped with It is configured to react with fuel such as heavy oil and concentrate falling from the concentrate chute 19.
このような構成の精鉱バーナーにおいては、補
助燃料導入管21を経て供給される燃料の燃焼
は、自熔炉の反応塔における全体的な熱収支を改
善するという目的の他に、燃料が早く着火して燃
焼しそれによつて精鉱の着火を促進するという目
的を有する。しかしながら従来の自熔製錬用精鉱
バーナーにおいては、バーナーチツプ24に設け
られた酸素噴出孔23は噴射方向が鉛直下方に向
いて形成されていたため、燃料を早く着火させ精
鉱の着火を助けるという効果が充分でなく、その
ため前記したフオーカスの位置を反応塔内の上部
に形成するという目的が達成できないという問題
があつた。 In the concentrate burner having such a configuration, the combustion of the fuel supplied through the auxiliary fuel inlet pipe 21 not only improves the overall heat balance in the reaction tower of the flash furnace, but also allows the fuel to ignite quickly. The purpose is to burn the concentrate, thereby promoting the ignition of the concentrate. However, in the conventional concentrate burner for self-melting smelting, the oxygen injection hole 23 provided in the burner chip 24 was formed with the injection direction facing vertically downward, which ignited the fuel quickly and helped ignite the concentrate. This effect was not sufficient, and there was a problem in that the above-mentioned objective of forming the focus at the upper part of the reaction column could not be achieved.
〔考案が解決しようとする課題〕
本考案の目的は、上記のような従来の自熔製錬
用精鉱バーナーの欠点を解消して、補助燃料が吹
き込まれた酸素によつて早く着火燃焼し、それに
よつて精鉱の着火を促進し、その結果反応塔内の
フオーカスの位置を従来より上昇させることがで
きる自熔製錬用精鉱バーナーを提供することにあ
る。[Problem to be solved by the invention] The purpose of the invention is to solve the above-mentioned drawbacks of the conventional concentrate burner for self-smelting and smelting, and to quickly ignite and burn with the oxygen injected with auxiliary fuel. The object of the present invention is to provide a concentrate burner for self-melting smelting, which can thereby promote the ignition of concentrate and, as a result, can raise the position of the focus in the reaction tower compared to the conventional one.
本考案の課題解決の手段は、下端にベンチユリ
ー状の絞り部が形成されたバーナー本体と、該バ
ーナー本体の中央部にその先端が絞り部よりやゝ
下方に突出するように垂設された管状の精鉱シユ
ートと、該精鉱シユートの中心を貫通して設けら
れた酸素吹込み管と、該酸素吹込み管中を同心を
成すように貫通して該酸素吹込み管の下端まで延
長する補助燃料導入管とを備えた精鉱バーナーに
おいて、前記酸素吹込み管及び補助燃料導入管の
下端に、燃料噴出孔が中央に開口し、該燃料噴出
孔を取り巻いて、一方は噴射角度が燃料噴出孔の
方に傾斜し他方は噴射角度が鉛直下方又は酸素吹
込み管より外方に向つて傾斜する2群の酸素噴出
孔を具えたバーナーチツプを接合したものであ
る。
The means of solving the problem of the present invention consists of a burner body with a ventilate-shaped constriction formed at the lower end, and a tube-shaped tube vertically disposed in the center of the burner body so that its tip protrudes slightly below the constriction. a concentrate chute, an oxygen blowing pipe provided through the center of the concentrate chute, and extending concentrically through the oxygen blowing pipe to a lower end of the oxygen blowing pipe. In the concentrate burner equipped with an auxiliary fuel introduction pipe, a fuel injection hole is opened in the center at the lower end of the oxygen injection pipe and the auxiliary fuel introduction pipe, and one side has an injection angle that This burner chip has two groups of oxygen blowing holes, one inclined toward the blowing hole and the other having a spray angle vertically downward or outward from the oxygen blowing tube.
本考案の一具体例を、第1図、第2図、第3図
により詳細に説明する。
A specific example of the present invention will be explained in detail with reference to FIGS. 1, 2, and 3.
第1図は本考案の自熔製錬用精鉱バーナーの全
体を示す概略断面図、第2図はバーナーチツプの
近傍を示す縦断面図、第3図は同じく水平断面図
である。18はバーナー本体であり、下部がベン
チユリー状で絞られた形状を成しており、上部側
面には反応用空気導入口17が設けられている。 FIG. 1 is a schematic sectional view showing the whole concentrate burner for self-melting smelting of the present invention, FIG. 2 is a longitudinal sectional view showing the vicinity of the burner chip, and FIG. 3 is a horizontal sectional view. Reference numeral 18 denotes a burner main body, which has a bent ventilate shape at the lower part, and a reaction air inlet 17 is provided at the upper side surface.
バーナー本体18の中央部には精鉱シユート1
9が垂設されており、その下端部はバーナー本体
18のベンチユリー状絞り部よりやゝ下方に達し
ている。精鉱シユート19の中心に酸素吹込み管
20が貫通して設けられており、本実施例におい
てはその下端は精鉱シユート19よりやゝ下方に
突出している。酸素吹込み管20の中には補助燃
料導入管21が同心を成すように貫通して設けら
れており、その下部は酸素吹込み管20の下端ま
で延長している。なお、補助燃料導入管21は、
詳細には第2図、第3図に示すように、酸素吹込
み管の内管25に接して挿通されており、補助燃
料導入管21を酸素吹込み管20から抜き出すこ
とが可能なように設けられている。酸素吹込み管
20及び補助燃料導入管21の下端に接してバー
ナーチツプ26が接合されており、バーナーチツ
プ26の中央には、補助燃料導入管21と連通す
る燃料噴出孔27がその中心線に沿つて設けら
れ、燃料噴出孔27を取り巻いて、酸素吹込み管
20と連通するそれぞれ複数個の酸素噴出孔28
a及び酸素噴出孔28bが設けられている。酸素
噴出孔28aは、上部の酸素吹込み管20内への
開口部から、下部開口部は燃料噴出孔27の近傍
に開口するように傾斜して設けられており、酸素
吹込み管20を通じて供給される酸素は燃料噴出
孔27の下部開口の直下に噴射されるように形成
されている。又、酸素噴出孔28bは、上部の酸
素吹込み管20内への開口部から、下部開口部は
バーナーチツプ26の外周側へ傾斜して設けられ
ており、この酸素噴出孔28bより噴出される酸
素気流は酸素吹込み管20の外周を下方に延長し
て仮想面よりも外方に向くように形成されてい
る。 A concentrate chute 1 is located in the center of the burner body 18.
9 is provided vertically, and its lower end reaches slightly below the ventilate-shaped constriction portion of the burner body 18. An oxygen blowing pipe 20 is provided through the center of the concentrate chute 19, and in this embodiment, its lower end protrudes slightly below the concentrate chute 19. An auxiliary fuel introduction pipe 21 is provided concentrically through the oxygen injection pipe 20, and its lower portion extends to the lower end of the oxygen injection pipe 20. Note that the auxiliary fuel introduction pipe 21 is
Specifically, as shown in FIGS. 2 and 3, the auxiliary fuel introduction pipe 21 is inserted through the inner pipe 25 of the oxygen injection pipe so that it can be extracted from the oxygen injection pipe 20. It is provided. A burner chip 26 is connected to the lower ends of the oxygen blowing pipe 20 and the auxiliary fuel introduction pipe 21, and a fuel injection hole 27 communicating with the auxiliary fuel introduction pipe 21 is located in the center of the burner chip 26 along its center line. A plurality of oxygen injection holes 28 are provided along the fuel injection hole 27, surround the fuel injection hole 27, and communicate with the oxygen injection pipe 20.
a and an oxygen jet hole 28b are provided. The oxygen nozzle 28a is provided at an angle such that the upper opening opens into the oxygen blowing pipe 20 and the lower opening opens near the fuel nozzle 27, so that the oxygen is supplied through the oxygen blowing pipe 20. The oxygen is injected directly below the lower opening of the fuel injection hole 27. Further, the oxygen ejection hole 28b is provided with an upper opening into the oxygen blowing pipe 20 and a lower opening inclined toward the outer circumferential side of the burner chip 26, and the oxygen is ejected from the oxygen injection hole 28b. The oxygen airflow is formed by extending the outer periphery of the oxygen blowing pipe 20 downward and facing outward from the imaginary plane.
尚、酸素噴出孔28aの噴射角度が燃料噴出孔
27の方へ傾斜して形成されていることは必らず
必要であるが、酸素噴出孔28bの噴射角度は鉛
直下方に向けて形成されていても酸素噴射量の多
い場合には本考案の目的を達する上で差支えがな
い。 Although it is absolutely necessary that the injection angle of the oxygen injection hole 28a is formed to be inclined toward the fuel injection hole 27, the injection angle of the oxygen injection hole 28b must be formed so as to be formed vertically downward. However, if the amount of oxygen injected is large, there is no problem in achieving the purpose of the present invention.
本考案の自熔製錬用精鉱バーナーは上記のよう
に構成されているので、酸素吹込み管20に酸素
を供給し、補助燃料導入管21に重油等の補助燃
料を供給しつつ、精鉱シユート19から硫化精鉱
を落下装入し反応用空気導入口17からは空気又
は酸素富化空気を送入しつつ自熔製錬炉の操業を
行なえば、バーナーチツプ26の燃料噴出孔27
から噴射された燃料は酸素噴出孔28aから燃料
噴出孔27の直近に噴射された酸素によつて、バ
ーナーチツプ26の直下で直ちに着火して燃焼
し、周囲に落下する硫化精鉱を加熱してその着火
を早める作用をする。そして、酸素噴出孔28b
から噴射された酸素は落下する硫化精鉱に供給さ
れてその着火を早めると共に、これを撹拌する作
用を為すことによつて反応用空気との接触を良く
し反応速度を早くする。
Since the concentrate burner for self-smelting smelting of the present invention is configured as described above, oxygen is supplied to the oxygen blowing pipe 20, and auxiliary fuel such as heavy oil is supplied to the auxiliary fuel introduction pipe 21, while refining If sulfide concentrate is dropped and charged from the ore chute 19 and air or oxygen-enriched air is introduced from the reaction air inlet 17 while the flash smelting furnace is operated, the fuel injection hole 27 of the burner chip 26
The fuel injected from the oxygen nozzle 28a immediately ignites and burns directly under the burner chip 26 due to the oxygen injected from the oxygen nozzle 28a to the vicinity of the fuel nozzle 27, heating the sulfide concentrate falling around it. It acts to hasten the ignition. And oxygen jet hole 28b
The oxygen injected from the sulfide concentrate is supplied to the falling sulfide concentrate to hasten its ignition, and by stirring it, it improves contact with the reaction air and speeds up the reaction rate.
従つて、精鉱シユート19から装入された硫化
精鉱は着火が早くなると共に反応速度が上るの
で、硫化精鉱の反応が最も活発で高温の領域であ
る反応塔内のフオーカスの位置が上昇する。 Therefore, the sulfide concentrate charged from the concentrate chute 19 ignites quickly and the reaction rate increases, so the position of the focus in the reaction tower, which is the area where the reaction of the sulfide concentrate is most active and high temperature, rises. do.
以上詳細に説明したように、本考案の自熔製錬
用精鉱バーナーによれば、従来は反応塔内のフオ
ーカスの位置を上昇させることが出来なかつたと
云う欠点を解消して、自熔製錬炉に装入された精
鉱の着火を早めると共にその反応速度を上昇させ
ることによつて、フオーカスの位置を上昇させる
ことができ、熔錬反応を効率的に行なわすことが
できるという効果がある。
As explained in detail above, the concentrate burner for autogenous smelting of the present invention solves the drawback of not being able to raise the focus position in the reaction tower in the past, and improves autosmelting. By speeding up the ignition of the concentrate charged into the smelting furnace and increasing its reaction rate, the position of the focus can be raised and the smelting reaction can be carried out efficiently. be.
第1図は本考案の自熔製錬用精鉱バーナーの全
体を示す概略断面図、第2図はバーナーチツプの
近傍を示す縦断面図、第3図は同じく水平断面図
である。第4図は従来の精鉱バーナーの概略断面
図であり、第5図は自熔炉の全体を示す説明図で
ある。
18……バーナー本体、19……精鉱シユー
ト、20……酸素吹込み管、21……補助燃料導
入管、26……バーナーチツプ、27……燃料噴
出孔、28a……酸素噴出孔、28b……酸素噴
出孔。
FIG. 1 is a schematic sectional view showing the entire concentrate burner for self-melting smelting of the present invention, FIG. 2 is a longitudinal sectional view showing the vicinity of the burner chip, and FIG. 3 is a horizontal sectional view. FIG. 4 is a schematic sectional view of a conventional concentrate burner, and FIG. 5 is an explanatory view showing the entire flash melting furnace. 18... Burner body, 19... Concentrate chute, 20... Oxygen blowing pipe, 21... Auxiliary fuel introduction pipe, 26... Burner chip, 27... Fuel injection hole, 28a... Oxygen injection hole, 28b ...Oxygen vent.
Claims (1)
ーナー本体と、該バーナー本体の中央部にその先
端が絞り部よりやゝ下方に突出するように垂設さ
れた管状の精鉱シユートと、該精鉱シユートの中
心を貫通して設けられた酸素吹込み管と、該酸素
吹込み管中を同心を成すように貫通して該酸素吹
込み管の下端まで延長する補助燃料導入管とを備
えた精鉱バーナーにおいて、前記酸素吹込み管及
び補助燃料導入管の下端に接合され、燃料噴出孔
が中央に開口し、該燃料噴出孔を取り巻いて、一
方は噴射角度が燃料噴出孔の方に傾斜し他方は噴
射角度が鉛直下方又は酸素吹込み管より外方に向
つて傾斜する2群の酸素噴出孔を具えたバーナー
チツプを有する自熔製錬用精鉱バーナー。 A burner body with a ventilate-shaped constriction formed at the lower end, a tubular concentrate chute hanging down from the center of the burner body so that its tip protrudes slightly below the constriction, and the concentrate. A precision fuel injection pipe having an oxygen blowing pipe provided through the center of the chute, and an auxiliary fuel inlet pipe passing concentrically through the oxygen blowing pipe and extending to the lower end of the oxygen blowing pipe. In the ore burner, the oxygen injection pipe and the auxiliary fuel introduction pipe are connected to the lower ends, a fuel injection hole opens in the center, surrounds the fuel injection hole, and one side has an injection angle inclined toward the fuel injection hole. The other is a concentrate burner for autosmelting, which has a burner chip equipped with two groups of oxygen injection holes whose injection angles are inclined vertically downward or outward from the oxygen blowing pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8598688U JPH0443701Y2 (en) | 1988-06-29 | 1988-06-29 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8598688U JPH0443701Y2 (en) | 1988-06-29 | 1988-06-29 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH027431U JPH027431U (en) | 1990-01-18 |
| JPH0443701Y2 true JPH0443701Y2 (en) | 1992-10-15 |
Family
ID=31310640
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8598688U Expired JPH0443701Y2 (en) | 1988-06-29 | 1988-06-29 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0443701Y2 (en) |
-
1988
- 1988-06-29 JP JP8598688U patent/JPH0443701Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPH027431U (en) | 1990-01-18 |
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