JPS6350408B2 - - Google Patents
Info
- Publication number
- JPS6350408B2 JPS6350408B2 JP14128085A JP14128085A JPS6350408B2 JP S6350408 B2 JPS6350408 B2 JP S6350408B2 JP 14128085 A JP14128085 A JP 14128085A JP 14128085 A JP14128085 A JP 14128085A JP S6350408 B2 JPS6350408 B2 JP S6350408B2
- Authority
- JP
- Japan
- Prior art keywords
- separation
- separation furnace
- furnace
- grains
- layer
- 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
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- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、〓とカワとを分離炉内で互いの比
重差によつて静置分離し、その後静置分離した〓
を上記分離炉側壁の〓取り出し口から取り出すよ
うにした〓の分離取り出し方法に関するものであ
る。[Detailed Description of the Invention] [Industrial Application Field] The present invention is a method of statically separating 〓 and carp based on the difference in their specific gravity in a separation furnace, and then statically separating 〓
The present invention relates to a method for separating and taking out the above-mentioned separation furnace by taking it out from the take-out port in the side wall of the separation furnace.
一般に、銅の連続製錬をなす場合には、銅鉱石
の予備処理、カワと〓との分離、粗銅の製造の各
工程を経て行なわれるが、ここで問題とする工程
は、カワと〓の分離工程である。この分離工程
は、たとえば、第3図に示すような分離炉1にお
いて行われる。この分離炉1は、中に流入する〓
2とカワ3とからなる溶湯を電極4,4によつて
通電加熱しながら〓2とカワ3とを静置分離する
ものであり、その側壁1aには、〓2を分離炉1
の外部に流出させる〓取り出し口5が形成され、
側壁1aと相対向する側壁1bの下端部には、カ
ワ取り出し口6が形成されている。なお、図中符
号7は、溶湯を分離炉1内に流入させるための溶
湯流入口である。
Generally, continuous smelting of copper is carried out through the following steps: preliminary treatment of copper ore, separation of copper and copper, and production of blister copper.The process in question here is the separation of copper and copper. This is a separation process. This separation step is performed, for example, in a separation furnace 1 as shown in FIG. This separation furnace 1 flows into the
The molten metal consisting of 2 and 3 is statically separated into 2 and 3 while being electrically heated by electrodes 4, 4.
An outlet 5 is formed to allow the flow to flow out to the outside.
A cloth removal port 6 is formed at the lower end of the side wall 1b facing the side wall 1a. Note that the reference numeral 7 in the figure is a molten metal inlet for flowing molten metal into the separation furnace 1.
上記の構成からなる分離炉1において互いの比
重差によつて静置分離された〓2とカワ3とのう
ち〓2は、〓取り出し口5から流出して取り出さ
れるとともに、カワ3は、カワ取り出し口6から
取り出される。 In the separation furnace 1 having the above-described configuration, the 2 and the sludge 3 are statically separated due to the difference in their specific gravity, and the 2 flows out from the outlet 5 and is taken out. It is taken out from the take-out port 6.
ところで、〓層の上表面には、未溶解の溶剤等
によつて形成された多数の浮遊物が浮遊してい
る。これら浮遊物は、多量のカワ粒を包含してい
るにもかかわらず〓と共に分離炉内から廃出され
るため歩留が悪いという問題があつた。また〓層
には、層流と完全混合流とからなる活性化部分が
存在し、完全混合流によつてカワ粒がまき上げら
れるため、カワ粒がカワ層に充分沈降せずに〓と
共に廃出され、このためより一層歩留りが悪いと
いう問題があつた。
By the way, a large number of floating substances formed by undissolved solvent and the like are floating on the upper surface of the layer. Although these floating substances contain a large amount of grains, they are discharged from the separation furnace along with the slag, resulting in a problem of poor yield. In addition, there is an activated part in the 〓 layer that consists of laminar flow and a completely mixed flow, and because the completely mixed flow stirs up the grains, the 〓 grains do not settle sufficiently in the 〓 layer and are discarded together with the 〓. Therefore, there was a problem that the yield was even worse.
なお、上記のような問題を解決する方法とし
て、分離炉内の溶湯の温度を上げて〓の粘度を下
げ、これによつて、浮遊物および〓中に含まれて
いるカワ粒を速やかにカワ層に沈降させ、〓と共
に分離炉内から廃出されるカワ粒の量を低減しよ
うとする方法が考えられる。 In addition, as a method to solve the above problems, the temperature of the molten metal in the separation furnace is raised to lower the viscosity of the molten metal, thereby quickly evaporating the suspended matter and the grains contained in the molten metal. A possible method is to reduce the amount of grains that are discharged from the separation furnace together with the grains by settling them into a layer.
ところが、このような方法では、消費電力量が
増え、そのためにエネルギー原単位が大きくな
り、また、電極の消耗や溶湯からの放散熱よる炉
壁の溶損等による消耗部材費および補修費用が増
大するという問題がある。 However, with this method, power consumption increases, which increases the energy consumption rate, and the cost of consumable parts and repair costs increase due to electrode wear and furnace wall melting due to heat dissipated from the molten metal. There is a problem with doing so.
この発明は、上記浮遊物および〓中に含まれる
カワ粒を速やかにカワ層に沈降させることがで
き、したがつて歩留りが良く、しかも消費電力が
少くて済み、また、電極の消耗や炉壁の溶損が少
い連続製錬工程における〓の分離取り出し方法を
提供するものである。 This invention allows the above-mentioned floating matter and the grains contained in the grain to quickly settle into the grain layer, resulting in a high yield and low power consumption. The present invention provides a method for separating and extracting 〓 in a continuous smelting process that causes less erosion loss of 〓.
この発明では、〓とカワとを分離炉内において
静置分離する際に、分離炉内の温度を降下させ、
それによつて〓の上表部に固化または半溶融化し
た表層部を形成することによつて上記問題を解決
している。
In this invention, when separating 〓 and carp while standing in a separation furnace, the temperature inside the separation furnace is lowered,
Thereby, the above problem is solved by forming a solidified or semi-molten surface layer on the upper surface.
浮遊物は、上記表層部と共に分離炉内に長時間
滞留し、その間に浮遊物に包含されたカワ粒がカ
ワ層に沈降するとともに、表層部によつて〓層の
活成化部分における層流の割合が増加し、それに
よつて、〓中のカワ粒は、まき上げられることな
くカワ層に速やかに沈降する。
The suspended solids remain in the separation furnace together with the surface layer for a long time, during which time the grains contained in the suspended solids settle into the carbon layer, and the surface layer creates a laminar flow in the activated part of the layer. As a result, the grains in the grains quickly settle into the grain layer without being thrown up.
以下、この発明の一実施例を第1図および第2
図を参照して説明する。
An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.
This will be explained with reference to the figures.
第1図は、〓とカワとが静置分離される分離炉
を示すものであり、その構成要素は、上記従来の
分離炉と同一のものを用いた。 FIG. 1 shows a separation furnace in which grains and ash are separated statically, and its components are the same as those of the conventional separation furnace described above.
この実施例においては、銅鉱石の前処理工程で
生成された〓25TON/Hrとカワ17TON/Hrか
らなる溶湯を溶湯流入口7から分離炉1内に連続
的に流入させながら電極4,4によつて通電加熱
した。このときの電極電圧は110Vに設定し、従
来よりも10V低く設定した。また、電極電流は、
従来と同じ設定で7.5KAとした。これによつて、
分離炉1内の温度は従来よりも低い温度になつて
カワ2層の上表部は冷却され、固化した表層部9
となつた。 In this embodiment, a molten metal of 25 TON/Hr and 17 TON/Hr of copper ore generated in the copper ore pre-treatment step is continuously flowed into the separation furnace 1 from the molten metal inlet 7 and transferred to the electrodes 4, 4. Then, it was heated with electricity. The electrode voltage at this time was set to 110V, 10V lower than before. In addition, the electrode current is
It was set to 7.5KA with the same settings as before. By this,
The temperature inside the separation furnace 1 is lower than that in the past, and the upper surface of the Kawa 2 layer is cooled, and the solidified surface layer 9
It became.
なお、カワ粒を取り除かれた〓2は、表層部9
の下側を流れ、〓取り出し口5から流出して取り
出されるとともに、カワ3はカワ取り出し口6か
ら取り出される。 In addition, 〓2 from which the grains were removed is the surface layer 9.
The cloth 3 flows under the cloth, flows out from the take-out port 5 and is taken out, and the cloth 3 is taken out from the cloth take-out port 6.
上記実施例においては、表層部9と共に浮遊物
8,8…が分離炉1内に長時間滞留し、浮遊物
8,8…の〓取り出し口5からの流出は見られな
かつた。また、第2図に示すように、表層部9に
よつて、〓2層の活成化部分における層流の割合
が22%となり、それに対する廃出〓中の銅品位は
0.56%であつた。なお、従来の連続製錬工程にお
ける〓の分離取り出し方法において、〓層の活成
化部分における層流の割合は13%以下であり、そ
れに対する廃出〓中の銅品位が図中ハツチングで
示すように0.6%から0.7%であつた。 In the above embodiment, the floating substances 8, 8, . Furthermore, as shown in Figure 2, due to the surface layer 9, the ratio of laminar flow in the activated part of the second layer is 22%, and the copper grade in the waste discharge is 22%.
It was 0.56%. In addition, in the conventional continuous smelting process, the ratio of laminar flow in the activated part of the layer is less than 13%, and the copper grade in the waste is shown by hatching in the figure. It was 0.6% to 0.7%.
また、表層部9は、保温材としての役割を奏
し、〓2およびカワ3の温度が125℃程度に保持
されており、〓2の粘度が上昇してカワ粒の沈降
が妨げられることはなかつた。 In addition, the surface layer 9 plays a role as a heat insulating material, and the temperature of the grains 2 and 3 is maintained at about 125°C, so that the viscosity of the grains 2 does not increase and the sedimentation of the grains is not hindered. Ta.
そして、さらに電極4,4間の電圧を110Vに
したことによつて、消費電力量を約200KWH低
減することができ、また、電極の消費量も従来の
約半分にすることができた。 Furthermore, by setting the voltage between the electrodes 4 to 110V, the power consumption could be reduced by about 200 KWH, and the consumption of the electrodes could also be reduced to about half of the conventional one.
この発明による連続製錬工程における〓の分離
取り出し方法においては、〓とカワとを分離炉内
において静置分離する際に、分離炉内の温度を降
下させ、それによつて〓の上表部に固化または半
溶融した表層部を形成することによつて、浮遊物
および〓中に含まれるカワ粒を速やかにカワ層に
沈降させることができ、したがつて歩留りが良
く、しかも消費電力が少くて済み、また、電極の
消耗や炉壁の溶損を少くすることができるという
効果を得ることができる。
In the method for separating and extracting 〓 in the continuous smelting process according to the present invention, when 〓 and millet are left to separate in the separation furnace, the temperature inside the separation furnace is lowered, thereby causing the upper surface of 〓 By forming a solidified or semi-molten surface layer, suspended matter and grains contained in the slag can be quickly settled into the sludge layer, resulting in a high yield and low power consumption. Moreover, it is possible to obtain the effect of reducing the wear of the electrodes and the melting damage of the furnace wall.
第1図および第2図はこの発明の一実施例を示
す図であつて、第1図は分離炉内において、〓の
上表部に固化した表層部が形成された状態を示す
図、第2図は分離炉内での〓層の活成化部分にお
ける層流の割合と分離炉内から廃出された〓の銅
品位との関係を示す線図、第3図は従来の連続製
錬工程における〓の分離取り出し方法において、
〓とカワとを分離炉内で静置分離している状態を
示す図である。
1……分離炉、1a……側壁、2……〓、3…
…カワ、5……〓取り出し口、9……表層部。
1 and 2 are diagrams showing one embodiment of the present invention, and FIG. 1 is a diagram showing a state in which a solidified surface layer portion is formed on the upper surface portion of the grain in a separation furnace, and FIG. Figure 2 is a diagram showing the relationship between the ratio of laminar flow in the activated part of the layer in the separation furnace and the copper grade of the copper discharged from the separation furnace. In the separation and extraction method of 〓 in the process,
FIG. 2 is a diagram showing a state in which 〓 and gloss are separated while standing in a separation furnace. 1...Separation furnace, 1a...Side wall, 2...〓, 3...
...Rubber, 5... Outlet, 9... Surface layer.
Claims (1)
て静置分離し、その後上記〓を上記分離炉の側壁
に形成された〓取り出し口から流し出して取り出
すようにした連続製錬工程における〓の分離取り
出し方法において、上記分離炉内の温度を降下さ
せることによつて、上記〓の上表部に固化または
半溶融化した表層部を形成することを特徴とする
連続製錬工程における〓の分離取り出し方法。1. A continuous smelting process in which the 〓 and the steel are separated by standing in a separation furnace based on the difference in their specific gravity, and then the 〓 is poured out and taken out from the 〓 outlet formed on the side wall of the separation furnace. In the continuous smelting process, which is characterized in that a solidified or semi-molten surface layer is formed on the upper surface of the 〓 by lowering the temperature in the separation furnace in the separation and extraction method of 〓. How to separate and take out 〓.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14128085A JPS621831A (en) | 1985-06-27 | 1985-06-27 | Method for separating and taking out slag in continuous smelting process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14128085A JPS621831A (en) | 1985-06-27 | 1985-06-27 | Method for separating and taking out slag in continuous smelting process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS621831A JPS621831A (en) | 1987-01-07 |
| JPS6350408B2 true JPS6350408B2 (en) | 1988-10-07 |
Family
ID=15288218
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14128085A Granted JPS621831A (en) | 1985-06-27 | 1985-06-27 | Method for separating and taking out slag in continuous smelting process |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS621831A (en) |
-
1985
- 1985-06-27 JP JP14128085A patent/JPS621831A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS621831A (en) | 1987-01-07 |
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