JP3144622B2 - Metal material melting furnace and melting method - Google Patents
Metal material melting furnace and melting methodInfo
- Publication number
- JP3144622B2 JP3144622B2 JP09951896A JP9951896A JP3144622B2 JP 3144622 B2 JP3144622 B2 JP 3144622B2 JP 09951896 A JP09951896 A JP 09951896A JP 9951896 A JP9951896 A JP 9951896A JP 3144622 B2 JP3144622 B2 JP 3144622B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- copper
- metal material
- combustion burner
- melting
- 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
Links
- 238000002844 melting Methods 0.000 title claims description 46
- 230000008018 melting Effects 0.000 title claims description 44
- 239000007769 metal material Substances 0.000 title claims description 19
- 238000000034 method Methods 0.000 title claims description 11
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 40
- 239000010949 copper Substances 0.000 claims description 40
- 229910052802 copper Inorganic materials 0.000 claims description 38
- 239000000295 fuel oil Substances 0.000 claims description 26
- 238000002485 combustion reaction Methods 0.000 claims description 21
- 238000005266 casting Methods 0.000 claims description 17
- 238000005868 electrolysis reaction Methods 0.000 claims description 11
- 239000002184 metal Substances 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 238000007664 blowing Methods 0.000 claims description 6
- 238000007670 refining Methods 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- 238000004090 dissolution Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 description 7
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000011978 dissolution method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000005058 metal casting Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、銅片を溶解して鋳
造用の溶湯を得る溶解炉及び溶解方法に係り、特に、電
解後のアノード板等鋳造に必要とされる純度を既に有し
ている銅片を再度溶解してアノード鋳造用の溶湯を得る
PS転炉を転用した溶解炉及び溶解方法に関する。The present invention relates to relates to a melting furnace and dissolution method to obtain a melt for casting by dissolving copper strip, in particular, electrostatic
The present invention relates to a melting furnace and a melting method in which a PS converter for obtaining a molten metal for anode casting by re-melting a copper piece having a purity required for casting such as an anode plate after melting is converted.
【0002】[0002]
【従来の技術】周知のように、PS転炉では、硫化物の
酸化熱を利用するため燃料は使用せず、従って、燃料を
PS転炉に導入するための構成は存在しない。PS転炉
からの溶湯は、精製炉に導かれ、酸化精練により不純物
を除去した後、天然ガス、アンモニアなどで還元し、純
度を99.8%に上げてから電解精製工程で用いる電極
板(アノード板)の形状に鋳造される。このアノード板
は、種板を陰極として電解精練される。所定形状のアノ
ード板は、電解精製工程で電解液中に溶け出し、電解前
の陽極質量に対する電解後の陽極質量の重量百分率は、
通常15〜20%である。2. Description of the Related Art As is well known, PS converters do not use fuel because they utilize the heat of oxidation of sulfides, and thus there is no arrangement for introducing fuel into the PS converter. The molten metal from the PS converter is guided to a refining furnace, where impurities are removed by oxidizing and scouring, and then reduced with natural gas, ammonia, etc. to increase the purity to 99.8%, and then used in an electrode plate ( (Anode plate). This anode plate is electrolytically refined using the seed plate as a cathode. The anode plate of a predetermined shape is dissolved in the electrolytic solution in the electrolytic purification step, and the weight percentage of the anode mass after electrolysis with respect to the anode mass before electrolysis is
Usually, it is 15 to 20%.
【0003】陰極銅は(Cu99.99%、電気銅)は
そのまま市販もするが、精銅反射炉で溶融し、Sなどの
不純物を除去、酸素含有量の調整を行い、適当な鋳型に
鋳込んで電線製造用の棹銅、型銅として市販する。一
方、電解後のアノード板は、Cuの純度が99.8%の
粗銅でままであるが、これらは通常PS転炉にて吹錬中
に発生する過剰酸化熱を緩和するための冷却材として転
炉内に投入される。[0003] Cathode copper (Cu 99.99%, electrolytic copper) is commercially available as it is, but it is melted in a refined copper reverberatory furnace, impurities such as S are removed, the oxygen content is adjusted, and cast into an appropriate mold. It is marketed as rod copper and mold copper for electric wire production. On the other hand, the anode plate after electrolysis is still blister copper having a Cu purity of 99.8%, but these are usually used as coolants for relaxing excessive heat of oxidation generated during blowing in a PS converter. It is put into the converter.
【0004】[0004]
【発明が解決しようとする課題】上述した従来技術で
は、自溶炉から鋳造設備までの一連のアノード板製造設
備において、自溶炉補修時に発生する鋳直しアノードを
処理することができず、鋳直しのための溶解炉及び鋳造
設備が別途必要であった。従って、設備費、人件費、管
理費などがその分余計にかかりこととなり不経済であっ
た。In the above-mentioned prior art, in a series of anode plate manufacturing equipment from the flash furnace to the casting equipment, the recast anode generated during the repair of the flash furnace cannot be processed. A separate melting furnace and casting equipment were needed. Therefore, equipment costs, personnel costs, management costs, and the like are extra, which is uneconomical.
【0005】一方、銅素材の需要はその時々の社会情勢
によって大きくかわるものであるが、銅の生産設備は需
要が拡大した時にも対応できるようにやや多めに建設さ
れている。従って、需要の落ち込んだ場合には、遊休設
備が生じることとなり、それらの有効活用が求められて
いる。[0005] On the other hand, the demand for copper material varies greatly depending on the social situation at the time, but copper production facilities are constructed a little more so as to be able to cope with an increase in demand. Therefore, when demand decreases, idle facilities are generated, and effective utilization of these facilities is required.
【0006】また、鋳直し用の溶解炉及び鋳造設備を設
けた場合、これらは一連のアノード板製造設備に比べて
規模が小さくて良く、従って、通常は一つずつしか建設
されない。しかし、これら鋳直し用の溶解炉及び鋳造設
備は、自溶炉補修時以外は遊休設備となってしまう欠点
があった。[0006] Further, when a melting furnace and a casting facility for recasting are provided, these can be smaller in size than a series of anode plate manufacturing facilities, and therefore, usually only one piece is constructed. However, these melting furnaces and casting facilities for recasting have a drawback that they become idle facilities except during the repair of the flash smelting furnace.
【0007】本発明は、上述した従来技術の課題に鑑み
なされたもので、既存の金属材料製造設備の内PS転炉
を用いて、従って、新たな設備投資を最小限に抑えると
共に最小限の人員及び管理により、電解後のアノード板
等鋳造に必要とされる純度を既に有している銅片を再度
溶解してアノード鋳造用の溶湯を得るPS転炉を転用し
た溶解炉及び溶解方法を提供することを目的とする。[0007] The present invention has been made in view of the above-mentioned problems of the prior art, and uses a PS converter in an existing metal material production facility, and thus minimizes new capital investment and minimizes capital investment. Anode plate after electrolysis by personnel and management
It is an object of the present invention to provide a melting furnace and a melting method in which a PS converter for obtaining a molten metal for anode casting by melting a copper piece having a purity required for equal casting again is used.
【0008】[0008]
【課題を解決するための手段】本発明は、電解後のアノ
ード板等鋳造に必要とされる純度を既に有している銅片
を再度溶解してアノード鋳造のための溶湯を得るための
金属材料の溶解炉であって、銅片を投入する入口と炉体
の回転軸方向に複数の羽口とを有するPS転炉を用い、
複数の羽口の一部をエア供給源から分離すると共に燃焼
バーナを装着して炉体内に火炎を噴射し、一方、該燃焼
バーナを装着した羽口の回転軸方向両側の羽口は燃焼バ
ーナ使用時に二次エアの吹込口として用いたことを特徴
とする金属材料の溶解炉を提供する。SUMMARY OF THE INVENTION The present invention provides an anolyte after electrolysis.
A metal material melting furnace for re-melting a copper piece having the purity required for casting such as a metal plate to obtain a molten metal for anode casting, and an inlet for charging the copper piece; Using a PS converter having a plurality of tuyeres in the rotation axis direction of the furnace body,
A flame injected into the furnace body by a part of the plurality of tuyeres mounted combustion burner with separate from the air supply source, while the rotation axis direction on both sides of the tuyere of the tuyere wearing the combustion burner combustion Bas
The present invention provides a melting furnace for a metal material, wherein the melting furnace is used as a secondary air inlet when using a furnace.
【0009】請求項2に記載の発明は、請求項1に記載
の金属材料の溶解炉において、前記PS転炉の入口に隣
接して銅片を投入するシュートを設けると共に、前記入
口から投入された銅片と衝接して該銅片を炉体内に分散
して飛散させる偏向板が設置されていることを特徴とす
る。According to a second aspect of the present invention, in the metal material melting furnace according to the first aspect, a chute for charging a copper piece is provided adjacent to an inlet of the PS converter, and a chute is charged from the inlet. was then copper piece and abutment, characterized in that the deflecting plate is scattered by dispersing the copper pieces to the furnace body is provided.
【0010】請求項3に記載の発明は、請求項1又は2
に記載の金属材料の溶解炉において、燃焼バーナを装着
した羽口を所定間隔毎に設け、その回転軸方向両側の少
なくとも2つの羽口は二次エアの吹込口とされてなるこ
とを特徴とする。[0010] The invention described in claim 3 is the invention according to claim 1 or 2.
In the metal material melting furnace described in the above, the tuyere equipped with a combustion burner is provided at predetermined intervals, at least two tuyeres on both sides in the rotation axis direction are formed as secondary air blowing ports. I do.
【0011】請求項4に記載の発明は、請求項1〜3の
いずれか1項に記載の金属材料の溶解炉において、炉体
の中央側の燃焼バーナから噴射される重油の圧力を炉体
の両外側の燃焼バーナから噴射される重油の圧力よりも
大きくしてその部位における燃焼バーナからの火炎の長
さを長くしたことを特徴とする。According to a fourth aspect of the present invention, in the melting furnace for a metal material according to any one of the first to third aspects, the pressure of heavy oil injected from a combustion burner at the center of the furnace body is reduced. The pressure of heavy oil injected from the combustion burners on both outer sides is made larger to extend the length of the flame from the combustion burner at that portion.
【0012】請求項5に記載の発明は、銅の精錬に使用
されるPS転炉を、アノード鋳直し用の溶解炉として用
いることを特徴とする金属材料の溶解方法を提供する。According to a fifth aspect of the present invention, there is provided a method for melting a metal material, wherein a PS converter used for refining copper is used as a melting furnace for recasting an anode .
【0013】請求項6に記載の発明は、請求項5に記載
の金属材料の溶解方法において、PS転炉の一部の羽口
をエア供給源から分離すると共に着脱可能な燃焼バーナ
の設置用として用い、少なくとも燃焼バーナが設置され
た該羽口の回転軸方向両側の羽口は二次エアの吹込口と
して用いることを特徴とする。According to a sixth aspect of the present invention, in the method for melting a metal material according to the fifth aspect, a part of the tuyere of the PS converter is separated from an air supply source and the combustion burner is detachable.
At least a combustion burner is installed.
The tuyere on both sides in the rotation axis direction of the tuyere is used as a secondary air blowing port.
【0014】[0014]
【発明の実施の形態】以下、図面を用いて本発明に係る
金属材料の溶解炉及び溶解方法について詳細に説明す
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a melting furnace and a melting method of a metal material according to the present invention will be described in detail with reference to the drawings.
【0015】図1は、本発明に係る金属材料の溶解炉の
一実施形態の中央断面図であり、図2は、図1の溶解炉
の羽口の位置を概略的に示す水平横断面図である。FIG. 1 is a central cross-sectional view of one embodiment of a melting furnace for a metal material according to the present invention, and FIG. 2 is a horizontal cross-sectional view schematically showing a position of a tuyere of the melting furnace of FIG. It is.
【0016】図示された本発明に係る溶解炉1は、電解
後のアノード板である純度が99.8%の銅片を再度溶
解して電解精練用のアノード板に鋳造するための溶湯と
する溶解炉であり、自溶炉から鋳造設備までの一連のア
ノード板製造設備の内のPS転炉を転用したものであ
る。In the illustrated melting furnace 1 according to the present invention, a copper piece having a purity of 99.8%, which is an anode plate after electrolysis, is melted again to form a molten metal for casting on an anode plate for electrolytic refining. This is a melting furnace in which a PS converter in a series of anode plate manufacturing facilities from a flash furnace to a casting facility is diverted.
【0017】溶解炉1は、概略的に、銅片を投入する入
口12と回転軸方向に複数の羽口14とを有する円筒状
の炉体10と、入口12に隣接して設けられた銅片を投
入するシュート20と、そして、炉体10を転炉中心C
を中心として回転可能に支持するローラ支持装置30と
を備えている。PS転炉自体は、従来周知であるからこ
こでの詳細な説明は省略し、溶解炉1への転用を行うに
際してなされた設計変更に関連する構成についてのみ説
明する。The melting furnace 1 has a cylindrical furnace body 10 having an inlet 12 for feeding copper pieces and a plurality of tuyeres 14 in the direction of the rotation axis, and a copper furnace provided adjacent to the inlet 12. A chute 20 for charging pieces, and the furnace body 10 is connected to the converter center C
And a roller support device 30 rotatably supported around the roller. Since the PS converter itself is conventionally well known, a detailed description thereof will be omitted here, and only a configuration related to a design change made when diverting to the melting furnace 1 will be described.
【0018】図3に最も良く示されているように、従来
の羽口14は、内張りであるマグネシア又はクロム・マ
グネシア耐火れんが10a及び外皮10bとを貫通する
羽口管14aと、羽口管14aの外皮10b側の端部を
該外皮10bに固定するための取付部材14bと、取付
部材14bにフランジ結合された分枝管14cとを含ん
でいる。そして、分枝管14cの一方の管路には、盲プ
ラグ14dを螺合して閉鎖し、他方の管路には、フレキ
シブルホース42を介して空気又は酸素冨化空気を送り
込むためのダクト40が連結されている。As best shown in FIG. 3, a conventional tuyere 14 comprises a tuyere tube 14a penetrating a magnesia or chrome-magnesia refractory brick 10a and a shell 10b, and a tuyere tube 14a. And a branch pipe 14c flanged to the mounting member 14b for fixing an end on the outer skin 10b side to the outer skin 10b. A blind plug 14d is screwed into one branch of the branch pipe 14c and closed, and a duct 40 for feeding air or oxygen-enriched air through a flexible hose 42 to the other pipeline. Are connected.
【0019】図示された実施形態では、羽口14は、炉
体10の軸方向に合計48ケ設けられている(図3参
照)。本発明の特徴は、これら48ケの羽口14をほぼ
7つずつの組に分け、中央5組の各組の中央の羽口14
に、図4に示されているように、重油バーナ18を装着
する点にある。重油バーナ18の装着は、取付部材14
bから分枝管14cを取り外し、その代わりに、重油バ
ーナ18を羽口管14aに挿入して、専用のアダプタ1
4eにて固定することによって行われる。同時に、取り
外した分枝管14cに連結されていたフレキシブルホー
ス42のダクト40側の端部をダクト40から外し、ダ
クト40には盲プラグ14dを螺合して閉鎖する。In the illustrated embodiment, a total of 48 tuyeres 14 are provided in the axial direction of the furnace body 10 (see FIG. 3). A feature of the present invention is that these 48 tuyeres 14 are divided into approximately seven sets, and the center tuyeres 14 of each of the five central sets are set.
Next, as shown in FIG. 4, a heavy oil burner 18 is mounted. The mounting of the heavy oil burner 18 is performed by the mounting member 14.
b, the heavy oil burner 18 is inserted into the tuyere tube 14a, and the special adapter 1 is inserted.
This is performed by fixing at 4e. At the same time, the end on the duct 40 side of the flexible hose 42 connected to the detached branch pipe 14c is removed from the duct 40, and the blind plug 14d is screwed into the duct 40 and closed.
【0020】各重油バーナ18は、所定の圧力調節装
置、例えば、レギュレータ19aを介して加圧された重
油供給源19に連結されている。通常、銅片は、炉体1
0のほぼ中央に設けられた入口12から炉体10内に投
入される。従って、銅片は、炉体10の中央部分が山と
なり両端に向って少なくなるように分布する。その場
合、効率良く銅片を溶解するため、炉体10の中央部分
への重油の供給を端部よりも多くすることが好ましい。
具体的には、中央側の重油バーナ18へは高圧の重油
を、そして、両端側の重油バーナ18には低圧の重油を
供給するようにレギュレータ19aを調節する。あるい
は、炉体10の中央側に於ける重油バーナ18の設置間
隔を炉体10の両側に比べて短い間隔としても、中央部
に山となった銅片を効率良く溶解することができる。Each heavy oil burner 18 is connected to a pressurized heavy oil supply source 19 via a predetermined pressure adjusting device, for example, a regulator 19a. Usually, the copper piece is placed in the furnace 1
0 is introduced into the furnace body 10 from an inlet 12 provided substantially at the center. Therefore, the copper pieces are distributed such that the central portion of the furnace body 10 becomes a mountain and decreases toward both ends. In this case, in order to efficiently dissolve the copper pieces, it is preferable that the supply of heavy oil to the central portion of the furnace body 10 be larger than that of the end portion.
Specifically, the regulator 19a is adjusted so that high-pressure heavy oil is supplied to the heavy oil burner 18 on the center side and low-pressure heavy oil is supplied to the heavy oil burners 18 on both ends. Alternatively, even if the interval of installation of the heavy oil burners 18 on the center side of the furnace body 10 is shorter than the both sides of the furnace body 10, the copper pieces crested at the center can be efficiently melted.
【0021】図1に示された好ましい実施形態では、入
口12に耐火材から作られたフランジ付きの円筒状ライ
ナ20が装着されており、このライナ20に銅片を投入
するシュート21が設けられている。天井クレーンによ
るボードチャージにて銅片を装入すると、銅片はこのシ
ュート21を落下し転炉10内に分散して放出される。
このように、銅片は比較的均等に炉体10内に分散して
投入されるため、各重油バーナ18への重油の圧力調整
や重油バーナ18の設置間隔を精密に行わなくても、投
入された銅片を効率良く溶解することができる利点を有
する。In the preferred embodiment shown in FIG. 1, the inlet 12 is fitted with a flanged cylindrical liner 20 made of refractory material, and the liner 20 is provided with a chute 21 for charging copper pieces. ing. When copper pieces are loaded by board charge using an overhead crane, the copper pieces fall down this chute 21 and are dispersed and discharged into the converter 10.
As described above, since the copper pieces are relatively uniformly dispersed and charged into the furnace body 10, the copper pieces can be charged without adjusting the pressure of the heavy oil to each heavy oil burner 18 or precisely setting the interval between the heavy oil burners 18. This has the advantage that the removed copper pieces can be efficiently dissolved.
【0022】PS転炉では、操業中に発生するSO2は
ダクト13を通じて廃ガスと共にボイラに導かれ硫酸の
回収に用いられる。そのため、ダクト13に設けられた
マット投入用の開口13aは、操業中は、開閉可能な前
面フード15によって閉鎖されている。PS転炉を本発
明に従って転用する場合、銅片は重油バーナ18から噴
射される重油によって加熱されるものであるが、排気ガ
ス中にSO2は含まれていないため、通常ダクト13を
用いず外カバー吸引ダクト17aを通して排出される。
前面フード15の内側に、排ガスがダクト13へ流入す
るのを防止すると共に、この部位からの熱の放散を防止
するための開閉可能な内側カバー22を設けることが好
ましく、これにより重油の消費を減少することができ
る。In the PS converter, SO2 generated during operation is guided to a boiler together with waste gas through a duct 13 and used for recovering sulfuric acid. For this reason, the opening 13 a for mat insertion provided in the duct 13 is closed by the front hood 15 that can be opened and closed during operation. When the PS converter is diverted according to the present invention, the copper pieces are heated by the heavy oil injected from the heavy oil burner 18, but since the SO 2 is not contained in the exhaust gas, the copper pieces are usually used without using the duct 13. It is discharged through the cover suction duct 17a.
Inside the front hood 15, it is preferable to provide an openable and closable inner cover 22 for preventing exhaust gas from flowing into the duct 13 and preventing heat from escaping from this portion, thereby reducing consumption of heavy oil. Can be reduced.
【0023】次に、かかる溶解炉1を用いて電解後のア
ノード板を溶解する操業方法について説明する。Next, an operation method of melting the anode plate after electrolysis using the melting furnace 1 will be described.
【0024】自溶炉から鋳造設備までの一連のアノード
板製造設備には、通常、3〜5炉のPS転炉が設置され
ている。その内の1炉を本発明に従って金属材料の溶解
炉に転用する。Usually, 3 to 5 PS converters are installed in a series of anode plate manufacturing facilities from a flash furnace to a casting facility. One of the furnaces is diverted to a melting furnace for metallic materials according to the present invention.
【0025】内側カバー22、外カバー17及び前面フ
ード15を開けて、天井クレーンによるボードチャージ
にて上方から電解後のアノード板を投入する。その際、
アノード板はシュート21を滑り落ち炉体10内に均一
に分散する。2〜3分で約3トンのアノード板を投入
し、炉体10内の分散の具合を見て、さらに、2〜3分
で約3トンのアノード板を投入する。The inner cover 22, the outer cover 17, and the front hood 15 are opened, and the anode plate after the electrolysis is loaded from above by board charging using an overhead crane. that time,
The anode plate slides down the chute 21 and is uniformly dispersed in the furnace body 10. An anode plate of about 3 tons is charged in a few minutes, the degree of dispersion in the furnace body 10 is checked, and an anode plate of about 3 tons is further charged in a few minutes.
【0026】合計6トンのアノード板を投入した後、外
カバー17を閉め、内側カバー22及び前面フード15
を所定の位置まで閉めて排ガスがダクト13に流入する
のを防止して、外カバー吸引ダクト17aに吸引される
ようにする。重油バーナ18に重油を圧送すると共に、
その両側の羽口14から空気を噴射しアノード板を溶解
する。約54〜55分で全てのアノード板は溶解する
が、溶け残りがある場合には酸素富化空気を導入する。
このような操業を、一日あたり23時間行うと、月産4
000トンといわれる電解後のアノード板の総量を1炉
のPS転炉からの転用溶解炉で処理できることとなる。After the anode plate of a total of 6 tons is charged, the outer cover 17 is closed, and the inner cover 22 and the front hood 15 are closed.
Is closed to a predetermined position to prevent exhaust gas from flowing into the duct 13 and to be sucked into the outer cover suction duct 17a. While pumping heavy oil to the heavy oil burner 18,
Air is injected from the tuyeres 14 on both sides to melt the anode plate. In about 54 to 55 minutes, all anode plates are dissolved, but if there is undissolved oxygen-enriched air is introduced.
If such an operation is performed for 23 hours per day, the monthly output is 4
The total amount of the anode plate after the electrolysis, which is said to be 000 tons, can be processed in the smelting furnace from one PS converter.
【0027】[0027]
【発明の効果】本発明は、銅片を投入する入口と炉体の
回転軸方向に複数の羽口とを有するPS転炉を用い、複
数の羽口の一部をエア供給源から分離すると共に燃焼バ
ーナを装着して炉体内に火炎を噴射し、一方、該燃焼バ
ーナを装着した羽口の少なくとも回転軸方向両側の羽口
は燃焼バーナ使用時の二次エアの吹込口として用いたた
め、新たな設備投資を最小限に抑えると共に最小限の人
員及び管理により、電解後のアノード板等のように必要
とされる純度を既に有している銅片を再度溶解してアノ
ード鋳造用の溶湯を得る溶解炉及び溶解方法が提供され
る効果を有する。According to the present invention, a PS converter having an inlet for charging copper pieces and a plurality of tuyeres in the rotation axis direction of the furnace body is used, and a part of the plurality of tuyeres is separated from an air supply source. Along with installing a combustion burner and injecting a flame into the furnace body, on the other hand, at least the tuyere on both sides in the rotation axis direction of the tuyere equipped with the combustion burner was used as a secondary air blowing port when using the combustion burner , By minimizing new capital investment and with minimum manpower and management, copper pieces that already have the required purity, such as anode plates after electrolysis , are redissolved and anodized.
The present invention has an effect that a melting furnace and a melting method for obtaining a molten metal for metal casting are provided.
【0028】それにより、PS転炉に遊休設備が生じた
場合にそれらの有効活用が可能となり、あるいは、鋳直
し用の溶解炉及び鋳造設備が別途建設されている場合に
も、それらの補修時などに暫定的にPS転炉を有効利用
できる利点を有する。This makes it possible to use idle facilities in the PS converter effectively when they occur, or to repair them when a melting furnace and casting facility for recasting are separately constructed. For example, there is an advantage that the PS converter can be used effectively.
【図1】 本発明に係る金属材料の溶解炉の一実施形態
の中央断面図である。FIG. 1 is a central sectional view of one embodiment of a melting furnace for metal materials according to the present invention.
【図2】 図1の溶解炉の羽口の位置を概略的に示す水
平横断面図である。FIG. 2 is a horizontal cross-sectional view schematically showing a position of a tuyere of the melting furnace of FIG.
【図3】 図1の羽口付近の拡大断面図である。FIG. 3 is an enlarged cross-sectional view around the tuyere of FIG.
【図4】 図3の羽口に重油バーナを装着した状態の拡
大断面図である。4 is an enlarged sectional view of a state in which a heavy oil burner is mounted on the tuyere of FIG.
1 溶解炉 10 炉体 10a 耐火レンガ、10b 外皮 12 入口 13 ダクト 14 羽口 14a 羽口管、14b 取付部材、14c 分枝管 14d 盲プラグ、14e アダプタ 15 前面フード 18 重油バーナ 19 重油供給源 19a レギュレータ 20 シュート 20a 偏向板 30 ローラ支持装置 DESCRIPTION OF SYMBOLS 1 Melting furnace 10 Furnace body 10a Refractory brick 10b Skin 12 Inlet 13 Duct 14 Tuyere 14a Tuyere pipe, 14b Mounting member, 14c Branch pipe 14d Blind plug, 14e Adapter 15 Front hood 18 Fuel oil burner 19 Fuel oil supply 19a Regulator Reference Signs List 20 chute 20a deflection plate 30 roller support device
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−256833(JP,A) 特開 平6−50671(JP,A) (58)調査した分野(Int.Cl.7,DB名) F27B 1/16 C22B 9/16 C22B 15/06 F27B 1/20 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-6-256833 (JP, A) JP-A-6-50671 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) F27B 1/16 C22B 9/16 C22B 15/06 F27B 1/20
Claims (6)
る純度を既に有している銅片を再度溶解してアノード鋳
造のための溶湯を得るための金属材料の溶解炉であっ
て、銅片を投入する入口と炉体の回転軸方向に複数の羽
口とを有するPS転炉を用い、前記複数の羽口の一部を
エア供給源から分離すると共に燃焼バーナを装着して炉
体内に火炎を噴射し、一方、該燃焼バーナを装着した羽
口の回転軸方向両側の羽口は燃焼バーナ使用時の二次エ
アの吹込口として用いたことを特徴とする金属材料の溶
解炉。1. Dissolution of a metal material for re-dissolving a copper piece having a purity required for casting such as an anode plate after electrolysis to obtain a molten metal for anode casting. a furnace, using a PS converter having a plurality of tuyeres in the direction of the rotation axis of the inlet and furnace to inject copper strip, a portion of the plurality of tuyeres
Separated from the air supply source and fitted with a combustion burner, the flame was injected into the furnace. On the other hand, the tuyeres on the both sides in the rotation axis direction of the tuyere equipped with the combustion burner blow secondary air during use of the combustion burner. A melting furnace for metallic materials, which is used as a mouth.
入するシュートを設けると共に、前記入口から投入され
た銅片と衝接して該銅片を炉体内に分散して飛散させる
偏向板が設置されていることを特徴とする請求項1に記
載の金属材料の溶解炉。With wherein providing the chute to inject copper strip adjacent to the inlet of the PS converter, and copper piece and abutment inserted from said inlet deflection is scattered by dispersing the copper pieces to the furnace body The melting furnace of a metal material according to claim 1, wherein a plate is provided.
に設け、その回転軸方向両側の少なくとも2つの羽口は
二次エアの吹込口とされてなることを特徴とする請求項
1又は2に記載の金属材料の溶解炉。3. A tuyere equipped with a combustion burner is provided at predetermined intervals, and at least two tuyeres on both sides in the rotation axis direction are formed as secondary air blowing ports. 3. The melting furnace for a metal material according to 2.
る重油の圧力を炉体の両外側の燃焼バーナから噴射され
る重油の圧力よりも大きくしてその部位における燃焼バ
ーナからの火炎の長さを長くしたことを特徴とする請求
項1〜3のいずれか1項に記載の金属材料の溶解炉。4. The pressure of heavy oil injected from a combustion burner on the center side of the furnace body is set to be higher than the pressure of heavy oil injected from combustion burners on both outer sides of the furnace body, so that the flame from the combustion burner at that portion is reduced. The melting furnace of a metal material according to any one of claims 1 to 3, wherein the length is increased.
ード鋳直し用の溶解炉として用いることを特徴とする金
属材料の溶解方法。5. A PS converter for use in refining of copper anode
A method for melting a metal material, wherein the method is used as a melting furnace for recasting a metal.
分離すると共に燃焼バーナの設置用として用い、燃焼バ
ーナが設置された該羽口の回転軸方向両側の羽口は二次
エアの吹込口として用いることを特徴とする請求項5に
記載の金属材料の溶解方法。6. A tuyere of a part of a PS converter is supplied from an air supply source.
Used for the installation of a combustion burner with separate combustion Bas
The method according to claim 5, wherein the tuyeres provided on both sides of the tuyere in the rotation axis direction are used as secondary air blowing ports.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09951896A JP3144622B2 (en) | 1996-03-29 | 1996-03-29 | Metal material melting furnace and melting method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09951896A JP3144622B2 (en) | 1996-03-29 | 1996-03-29 | Metal material melting furnace and melting method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09269191A JPH09269191A (en) | 1997-10-14 |
| JP3144622B2 true JP3144622B2 (en) | 2001-03-12 |
Family
ID=14249477
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP09951896A Expired - Fee Related JP3144622B2 (en) | 1996-03-29 | 1996-03-29 | Metal material melting furnace and melting method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3144622B2 (en) |
-
1996
- 1996-03-29 JP JP09951896A patent/JP3144622B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09269191A (en) | 1997-10-14 |
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