JP2019143209A - Operation method of metal refining furnace - Google Patents

Operation method of metal refining furnace Download PDF

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JP2019143209A
JP2019143209A JP2018029338A JP2018029338A JP2019143209A JP 2019143209 A JP2019143209 A JP 2019143209A JP 2018029338 A JP2018029338 A JP 2018029338A JP 2018029338 A JP2018029338 A JP 2018029338A JP 2019143209 A JP2019143209 A JP 2019143209A
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furnace
furnace body
displacement
upper limit
metal
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JP6913043B2 (en
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竜也 本村
Tatsuya Motomura
竜也 本村
友也 川崎
Tomoya Kawasaki
友也 川崎
武英 行里
Takehide YUKISATO
武英 行里
裕史 千田
Yasushi Senda
裕史 千田
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Pan Pacific Copper Co Ltd
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Pan Pacific Copper Co Ltd
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Priority to JP2018029338A priority Critical patent/JP6913043B2/en
Priority to PCT/JP2019/005123 priority patent/WO2019163607A1/en
Priority to CN201980001817.1A priority patent/CN110475881B/en
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B5/00General methods of reducing to metals
    • C22B5/02Dry methods smelting of sulfides or formation of mattes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D21/00Arrangements of monitoring devices; Arrangements of safety devices

Abstract

To provide an operation method of a metal refining furnace capable of suppressing deformation of a furnace body due to expansion of a refractory of the metal refining furnace.SOLUTION: Variation measurements 8to 8are arranged per prescribed interval around a furnace body 2, variation of whole furnace body 2 is measured periodically at prescribed timing, and control to reduce an operation temperature in a furnace 2 is conducted so that the variation of the furnace body 2 is upper limit or less when variation of at least one location is over preset upper limit, and renewal timing of the furnace body 2 is determined from remaining linear expansion coefficient of the furnace body 2 and variation limitation of a frame constituting the furnace. Thereby expansion or deformation of the furnace body 2 can be maintained in prescribed range, and further renewal of a furnace material becomes available at proper timing.SELECTED DRAWING: Figure 1

Description

本発明は、金属精錬炉の操業方法に関し、さらに詳しくは、例えば、銅精錬における自溶炉をはじめとする金属精錬炉の耐火物の膨張による炉体の変形を抑制することが可能な金属精錬炉の操業方法に関する。   The present invention relates to a method for operating a metal smelting furnace, and more particularly, for example, metal smelting capable of suppressing deformation of a furnace body due to expansion of a refractory in a metal smelting furnace including a flash smelting furnace in copper refining. It relates to the operation method of the furnace.

金属精錬における金属精錬炉、例えば、銅精錬における自溶炉100は、図6に示すように、反応シャフト101、セットラ102及びアップテイク103から構成され、反応シャフト101には1〜3本の精鉱バーナ104,104が設けられている。そして、精鉱を酸素富化空気あるいは高温熱風と同時に吹き込んで瞬間的に化学反応を起こさせ、比重差によってマットとスラグに分離する。自溶炉100は精鉱の酸化反応熱を利用するため他の方法より燃料消費率が低いという特徴がある。処理する原料の品位、組成によっては、酸化反応熱だけでは熱量が不足することもあるため、精鉱バーナ104,104から重油等で助燃することもある。   A metal smelting furnace in metal smelting, for example, a flash smelting furnace 100 in copper smelting, is composed of a reaction shaft 101, a setter 102 and an uptake 103, as shown in FIG. Mining burners 104, 104 are provided. Then, the concentrate is blown simultaneously with oxygen-enriched air or high-temperature hot air to cause a chemical reaction instantaneously, and is separated into mat and slag by the specific gravity difference. The flash smelting furnace 100 is characterized by a lower fuel consumption rate than other methods because it uses the heat of oxidation reaction of concentrate. Depending on the quality and composition of the raw material to be processed, the amount of heat may be insufficient with only the oxidation reaction heat, and the concentrate burners 104 and 104 may be supplemented with heavy oil or the like.

マットには、通常、銅が60〜70%含まれており、このマットは自溶炉100の底部近傍に複数連設して設けられたマットタップホール105,105から抜き出される。一方、スラグには1%前後の銅が含まれているためアップテイク103の下部側に設けられたスラグタップホール106からスラグを抜き出して錬かん炉120へ送って錬かんし、スラグに含まれる銅をマットとして回収し、自溶炉100から抜き出されたマットとあわせて転炉で処理する。そして、電解精製によってさらに品位の高い電気銅が製造される。   The mat usually contains 60 to 70% of copper, and the mat is extracted from mat tap holes 105 and 105 provided in a row in the vicinity of the bottom of the flash smelting furnace 100. On the other hand, since the slag contains about 1% copper, the slag is extracted from the slag tap hole 106 provided on the lower side of the uptake 103 and sent to the smelting furnace 120 for smelting, and the copper contained in the slag. Is collected as a mat and is processed in a converter together with the mat extracted from the flash furnace 100. And electrolytic copper of higher quality is manufactured by electrolytic refining.

自溶炉をはじめとする銅精練炉のシェル(缶体)内部は、主に耐火レンガや不定形耐火物で構成されている。耐火物は操業中の高温状態では膨張し、定期修理(冷間補修)中のように長期操業停止した際には低温状態となって収縮する性質がある。これのような耐火物の熱膨張による炉体の変形は、炉体の健全性悪化につながることから変形状況の確認が必要となる。そして、上記のような高温状態と低温状態が繰り返されると、耐火物の残存線膨張により低温状態となって収縮しても元の大きさまでは戻らず、徐々に膨張が拡大する。そのため、冷間補修を実施する周期が短い炉ほど、耐火物の残存線膨張により、耐火物を保持する炉体フレームの変形や変位が大きくなる。さらに、耐火物中の特定の成分、例えば、MgOやCaOと水が接触すると水和物を形成して耐火物が急激に膨張し、最悪の場合には崩壊する、いわゆるスレーキングが発生する。このような耐火物の膨張は、炉底の耐火レンガの配列を崩したり、空隙を発生させたりすることによる湯漏れのリスクの増大や、炉体フレームの破損等のトラブルにつながるおそれがある。   The inside of a shell (can) of a copper smelting furnace including a flash smelting furnace is mainly composed of refractory bricks and irregular refractories. The refractory has a property of expanding at a high temperature during operation and contracting at a low temperature when the operation is stopped for a long time, such as during regular repair (cold repair). Such deformation of the furnace body due to the thermal expansion of the refractory leads to deterioration of the soundness of the furnace body, so it is necessary to confirm the deformation state. When the high temperature state and the low temperature state as described above are repeated, the expansion does not return to the original size even when the refractory material is contracted to a low temperature state due to the residual linear expansion, and the expansion gradually expands. Therefore, a furnace having a shorter cycle for performing cold repair has a larger deformation and displacement of the furnace frame holding the refractory due to the residual linear expansion of the refractory. Furthermore, when a specific component in the refractory, for example, MgO or CaO, comes into contact with water, a hydrate is formed and the refractory expands rapidly. In the worst case, so-called slaking occurs. Such expansion of the refractory may lead to troubles such as an increased risk of leakage due to the destruction of the arrangement of the refractory bricks at the bottom of the furnace or the generation of voids, and damage to the furnace frame.

そのため、従来、炉体が設置されている建物の支柱等を基準点とし、そして、炉体の所定の部分を目印として、その目印までの距離を定期的に測定し、炉体の膨張を監視することが行われていた。例えば、特許文献1では、コークス炉の炉体膨張計測方法が開示されている。   Therefore, conventionally, the pillar of the building where the furnace body is installed is used as a reference point, and a predetermined part of the furnace body is used as a mark, and the distance to the mark is periodically measured to monitor the expansion of the furnace body. It was done. For example, Patent Literature 1 discloses a method for measuring a furnace expansion of a coke oven.

特開平9−26309号公報JP-A-9-26309

しかしながら、従来の方法では、測定点を炉体の代表的な部分に絞って目印としていたため、変化に気付き難いといった問題があった。そのため、炉体の膨張や変形の発見が遅れ、補強等の対応が遅れることとなり、炉体を構成する部材のひび割れや破断につながるおそれがあった。   However, the conventional method has a problem that it is difficult to notice the change because the measurement point is focused on a representative portion of the furnace body as a mark. Therefore, the discovery of expansion and deformation of the furnace body is delayed, and the response such as reinforcement is delayed, which may lead to cracks and breakage of the members constituting the furnace body.

また、例えば、特許文献1に示す炉体膨張計測方法は、単に炉体の膨張や変形を発見するものであり、炉体の膨張や変形が早期に発見することができた場合であっても、それは適切な時点で補修等の対応を行うことが可能となるだけであって、炉体の膨張や変形それ自体を抑制・制御するものではない。   In addition, for example, the furnace body expansion measuring method shown in Patent Document 1 merely discovers the expansion and deformation of the furnace body, and even when the expansion and deformation of the furnace body can be discovered early. It is only possible to perform repairs or the like at an appropriate time, and does not suppress or control the expansion or deformation of the furnace body itself.

そこで、本発明は、かかる問題点に鑑みなされたもので、炉体の膨張や変形を適正な範囲内に維持することにより炉底の耐火レンガ配列の損傷による湯漏れのリスクの増大や、炉体フレームの変形や破損等のトラブルの発生を抑制することが可能な金属精錬炉の操業方法を提供することを目的とする。   Therefore, the present invention has been made in view of such problems, and by maintaining expansion and deformation of the furnace body within an appropriate range, the risk of hot water leakage due to damage to the refractory brick array at the bottom of the furnace, An object of the present invention is to provide a method for operating a metal refining furnace capable of suppressing the occurrence of troubles such as deformation and breakage of a body frame.

また、本発明は、経年的に生じる炉長変化を監視して適切なタイミングで炉材の更新を行うことを可能とする金属精錬炉の操業方法を提供することを目的とする。   It is another object of the present invention to provide a method for operating a metal refining furnace that enables a furnace material to be updated at an appropriate timing by monitoring a furnace length change that occurs over time.

上記課題を解決するため請求項1に記載の本発明は、炉体の膨張や変形を所定の範囲内に維持する金属精錬炉の操業方法において、複数の変位計によって前記炉体の所定の複数箇所の変位をそれぞれ計測し、少なくとも一箇所以上の変位が予め設定した上限値を超えることとなった場合には、当該変位が前記上限値以下となるように前記炉体内の操業温度を下げることを特徴とする。   In order to solve the above problems, the present invention according to claim 1 is a method for operating a metal refining furnace in which expansion and deformation of a furnace body are maintained within a predetermined range. Measure the displacement of each location, and if the displacement of at least one location exceeds the preset upper limit value, lower the operating temperature in the furnace so that the displacement is less than the upper limit value It is characterized by.

上記課題を解決するため請求項2に記載の本発明は、請求項1に記載の金属精錬炉の操業方法において、前記変位が予め設定した上限値を超えることとなった場合には、A.前記炉体に装入する原料について発熱量の小さい原料の混合比率を増加すること、B.前記炉体に装入する原料の時間当たりの装入量を減らすこと、C.前記炉体の冷却を行うこと、D.還元材の投入量を調整することによりセルフコーティングを形成しやすい炉内環境とすること、E.マット層中の銅品位(マットグレード(MG))を下げること、のいずれか又はA乃至Eのいずれかの組み合わせによって前記炉体内の操業温度を下げることを特徴とする   In order to solve the above-mentioned problem, the present invention as claimed in claim 2 is characterized in that, in the method for operating a metal smelting furnace as claimed in claim 1, when the displacement exceeds a preset upper limit value, B. Increasing the mixing ratio of raw materials with a small calorific value for the raw materials charged into the furnace body; C. reducing the amount of raw material charged into the furnace body per hour; C. cooling the furnace body; E. Adjusting the amount of reducing material to be in-furnace environment in which self-coating can be easily formed; The operation temperature in the furnace body is lowered by either reducing the copper quality (mat grade (MG)) in the mat layer, or any combination of A to E.

上記課題を解決するため請求項3に記載の本発明は、請求項1又は2に記載の金属精錬炉の操業方法において、前記変位計は、前記炉体の周囲に所定間隔ごとに配置し、前記炉体の全体の変位を計測することを特徴とする。   In order to solve the above-mentioned problem, the present invention described in claim 3 is the method for operating a metal refining furnace according to claim 1 or 2, wherein the displacement meters are arranged around the furnace body at predetermined intervals. The displacement of the whole furnace body is measured.

上記課題を解決するため請求項4に記載の本発明は、請求項3項に記載の金属精錬炉の操業方法において、前記変位計は、前記炉体の側壁を支持する各バックステイの変位を計測することを特徴とする。   In order to solve the above-mentioned problem, the present invention described in claim 4 is the method of operating a metal smelting furnace according to claim 3, wherein the displacement meter detects the displacement of each backstay that supports the side wall of the furnace body. It is characterized by measuring.

上記課題を解決するため請求項5に記載の本発明は、請求項1から4のいずれか1項に記載の金属精錬炉の操業方法において、前記上限値は、前記炉体が変位することによって当該炉体を構成するフレームに付加される荷重が当該フレームを塑性変形させる弾性限界を超えない変位であることを特徴とする。   In order to solve the above-mentioned problem, the present invention according to claim 5 is the method for operating a metal refining furnace according to any one of claims 1 to 4, wherein the upper limit value is obtained by displacing the furnace body. The load applied to the frame constituting the furnace body is a displacement not exceeding an elastic limit for plastically deforming the frame.

上記課題を解決するため請求項6に記載の本発明は、請求項1から5のいずれか1項に記載の金属精錬炉の操業方法において、前記変位計の計測値によって算出される前記炉体の残存線膨張率が所定の割合を超えた場合に前記炉体を形成する各種炉材の更新を行うことを特徴とする。   In order to solve the above-mentioned problem, the present invention according to claim 6 is the operation method of the metal refining furnace according to any one of claims 1 to 5, wherein the furnace body is calculated based on the measured value of the displacement meter. When the remaining linear expansion coefficient exceeds a predetermined ratio, the various furnace materials forming the furnace body are updated.

本発明に係る金属精錬炉の操業方法によれば、炉体フレームの塑性変形範囲内での操業が可能になることで、炉体の膨張や変形を適正な範囲内に維持できるという効果がある。   According to the method for operating a metal smelting furnace according to the present invention, it becomes possible to maintain the expansion and deformation of the furnace body within an appropriate range by enabling operation within the plastic deformation range of the furnace body frame. .

また、本発明は、経年的に生じる炉長変化を監視できることで、適切なタイミングで炉材の更新が可能になるという効果がある。   Further, the present invention has an effect that the furnace material can be renewed at an appropriate timing by monitoring the change in the furnace length that occurs over time.

本発明に係る操業方法を実施するための好ましい一実施形態の金属精練炉の構成を示す平面図である。It is a top view which shows the structure of the metal smelting furnace of preferable one Embodiment for enforcing the operating method which concerns on this invention. 図1の金属精練炉のA−A断面図である。It is AA sectional drawing of the metal smelting furnace of FIG. ジャケットの正面図である。It is a front view of a jacket. 変位計の出力に基づいて各種の制御を行う制御装置の構成を示すブロック図である。It is a block diagram which shows the structure of the control apparatus which performs various controls based on the output of a displacement meter. 本発明に係る金属精練炉の操業方法の一実施形態のフローチャートである。It is a flowchart of one Embodiment of the operating method of the metal smelting furnace which concerns on this invention. 銅精錬における自溶炉の一例を示す正面断面図である。It is front sectional drawing which shows an example of the flash smelting furnace in copper refining.

以下、本発明に係る金属精練炉の操業方法について、好ましい実施形態に基づいて詳細に説明する。まず、本発明に係る金属精練炉の操業方法を説明する前に、本発明が適用される金属精練炉の構成について説明する。図1は本発明に係る操業方法を実施するための好ましい一実施形態の金属精練炉の構成を示す平面図、図2は図1の金属精練炉のA−A断面図である。   Hereinafter, the operation method of the metal smelting furnace which concerns on this invention is demonstrated in detail based on preferable embodiment. First, before explaining the operation method of the metal smelting furnace according to the present invention, the configuration of the metal smelting furnace to which the present invention is applied will be described. FIG. 1 is a plan view showing a configuration of a metal smelting furnace of a preferred embodiment for carrying out the operating method according to the present invention, and FIG. 2 is a cross-sectional view taken along line AA of the metal smelting furnace of FIG.

[金属精練炉の構成]
図示された金属精練炉1は、いわゆる自溶炉であり、概略として、一端側に設けられた反応シャフト3と、他端側に設けられたアップテイク4と、反応シャフト3とアップテイク4の中間部に位置するセットラ5を備えて炉体2が構成されており、炉体2は、全体が鋼材等の金属製材料によって形成されたシェル(缶体)によって形成されている。そして、
炉体2には、必要な強度を確保するための補強材として複数のバックステイ2a,2aが周囲を取り囲むようにして所定間隔で配置されている。
[Configuration of metal smelting furnace]
The illustrated metal smelting furnace 1 is a so-called flash furnace, and generally includes a reaction shaft 3 provided on one end side, an uptake 4 provided on the other end side, a reaction shaft 3 and an uptake 4. A furnace body 2 is configured to include a setler 5 located at an intermediate portion, and the furnace body 2 is entirely formed by a shell (can body) formed of a metal material such as a steel material. And
In the furnace body 2, a plurality of backstays 2 a and 2 a are arranged at a predetermined interval so as to surround the periphery as reinforcing materials for ensuring necessary strength.

反応シャフト3は、略円筒形状とされ、その上部には複数の精鉱バーナ6,6が配置されている。そして、精鉱バーナ6,6に隣接するようにして予熱空気注入口7が設けられている。セットラ5は、図3に示すような水冷ジャケット30を複数連接することにより形成されている。水冷ジャケット30は、内部に冷却水を循環させる複数の冷却管32,32を備えると共に、各冷却管32,32の一端側にはそれぞれ冷却水を供給するための給水口33,33が設けられ、また、その他端側には冷却水を排出するための排水口34,34が設けられている。炉内側の表面には図示しない複数のリブが形成されており、リブには図示しない耐火レンガが積層される。アップテイク4は、内部の排ガスを廃熱ボイラへ誘導して廃熱の回収を行い、冷却された排ガスは硫酸工場に送られる。   The reaction shaft 3 has a substantially cylindrical shape, and a plurality of concentrate burners 6 and 6 are disposed on the reaction shaft 3. A preheating air inlet 7 is provided adjacent to the concentrate burners 6 and 6. The setler 5 is formed by connecting a plurality of water cooling jackets 30 as shown in FIG. The water cooling jacket 30 includes a plurality of cooling pipes 32 and 32 for circulating cooling water therein, and water supply ports 33 and 33 for supplying cooling water are provided on one end sides of the cooling pipes 32 and 32, respectively. In addition, drain ports 34 for discharging cooling water are provided on the other end side. A plurality of ribs (not shown) are formed on the inner surface of the furnace, and fire bricks (not shown) are stacked on the ribs. The uptake 4 recovers waste heat by guiding the internal exhaust gas to a waste heat boiler, and the cooled exhaust gas is sent to a sulfuric acid factory.

そして、炉体2の周囲には、所定間隔で炉体2を取り巻くようにして所要数(本実施形態では42個)の変位計8(以下、「変位計8−1〜8−42」ともいう。)が配置されている。これらの変位計8によって炉体2の全体の変位の計測を行う。尚、本実施形態では変位計8−1〜8−42は、膨張の大きい炉底レベルの炉体2に配置された42個の各バックステイ2aにそれぞれ対向配置させている。尚、変位計8,8の数は42個に限定されるものではなく、炉体2の形状、大きさ等に応じて適宜決定される。また、変位の計測はバックステイ2aに限るものではなく、炉体2の適宜の位置を目印にすることができる。 Around the furnace body 2, the required number (42 in the present embodiment) of displacement gauges 8 (hereinafter referred to as “displacement gauges 8 −1 to 8 −42 ”) surrounds the furnace body 2 at predetermined intervals. Say). These displacement gauges 8 measure the overall displacement of the furnace body 2. In the present embodiment, the displacement meters 8 −1 to 8 −42 are disposed to face the 42 backstays 2 a disposed in the furnace body 2 at the furnace bottom level where the expansion is large. Note that the number of displacement meters 8, 8 is not limited to 42, and is appropriately determined according to the shape, size, etc. of the furnace body 2. Further, the displacement measurement is not limited to the backstay 2a, and an appropriate position of the furnace body 2 can be used as a mark.

変位計8−1〜8−42は、炉体2の変位(膨張)を計測する光学式または物理式のセンサであり、計測した炉体2の変位量を長さに変換した電気信号を出力する。変位計8−1〜8−42には、例えば、レーザフォーカス式、超音波式、三角測距等の非接触方式や差動トランス式の接触方式等がある。 The displacement meters 8 −1 to 8 −42 are optical or physical sensors that measure the displacement (expansion) of the furnace body 2, and output an electrical signal obtained by converting the measured displacement amount of the furnace body 2 into a length. To do. Examples of the displacement meters 8 -1 to 8 -42 include a non-contact method such as a laser focus method, an ultrasonic method, and a triangulation, a contact method using a differential transformer, and the like.

図4は変位計の出力に基づいて各種の制御を行う制御装置の構成を示すブロック図である。制御装置10は、CPUやメモリ等によって構成され、変位計8−1〜8−42による計測値を一定時間毎に取り込み、その計測値に基づいて図5に示すフローを実行するプログラムを備えた演算部11を備えている。すなわち、制御部10は、変位計8−1〜8−42によって計測された炉体2の変位(膨張)が予め設定された上限の範囲内であるか否かを監視し、炉体2の変位(膨張)が予め設定された変位の上限を超えるような場合には変位(膨張)が上限値以下となるように操業温度を下げる制御を行う。そして、操業温度を下げる制御を実行するために以下のような制御系統が設けられている。すなわち、制御装置10は、演算部11からの指令に基づいて炉体2に装入する原料について発熱量の小さい原料、例えば、酸化鉄スラグの混合比率を増加する原料混合制御部12、演算部11からの指令に基づいて精鉱の時間当たりの装入量を制御する装入量制御部13、演算部11からの指令に基づいて炉体2の冷却を行う冷却制御部14、演算部11の指令に基づいて炉内に投入する還元材の投入量を制御する還元材投入制御部15を備えている。 FIG. 4 is a block diagram showing the configuration of a control device that performs various controls based on the output of the displacement meter. The control device 10 includes a CPU, a memory, and the like, and includes a program that takes in the measurement values obtained by the displacement meters 8 -1 to 8-42 at regular intervals and executes the flow illustrated in FIG. 5 based on the measurement values. A calculation unit 11 is provided. That is, the control unit 10 monitors whether or not the displacement (expansion) of the furnace body 2 measured by the displacement meters 8 -1 to 8-42 is within a preset upper limit range. When the displacement (expansion) exceeds a preset upper limit of displacement, control is performed to lower the operating temperature so that the displacement (expansion) is less than or equal to the upper limit value. And in order to perform control which lowers operating temperature, the following control systems are provided. That is, the control device 10 includes a raw material mixing control unit 12 that increases the mixing ratio of a raw material with a small calorific value, for example, iron oxide slag, with respect to the raw material charged into the furnace body 2 based on a command from the calculating unit 11, and a calculating unit. 11, a charging amount control unit 13 that controls the charging amount per time of concentrate based on a command from 11, a cooling control unit 14 that cools the furnace body 2 based on a command from the calculation unit 11, and a calculation unit 11. Is provided with a reducing material charging control unit 15 for controlling the amount of reducing material charged into the furnace.

ここで、上限値は、炉体2が変位することによって炉体2を構成するフレーム、例えば、バックステイ2aに付加される荷重がバックステイ2aを塑性変形させる弾性限界を超えない変位、好ましく弾性限界に対して一定の余裕をもたせた変位、例えば10%の余裕を持たせた変位とする。すなわち、耐火物は加熱されると膨張し、温度が下がると収縮するため、操業停止時には操業時よりも変位が小さくなるが耐火物の特性上完全に元に戻ることはなく、加熱冷却を繰り返すうちに加熱時の変位が大きくなり冷却してもその変位は次第に大きくなる。そして、炉体2が変位することによって炉体2を構成するフレーム、例えばバックステイ2aに付加される荷重がバックステイ2aを塑性変形させる弾性限界を超えることになった場合には操業温度を下げても炉体2は変形したままの状態となってしまうからである。   Here, the upper limit value is a displacement in which the load applied to the frame constituting the furnace body 2 by the displacement of the furnace body 2, for example, the backstay 2a does not exceed the elastic limit for plastically deforming the backstay 2a, preferably elastic A displacement having a certain margin with respect to the limit, for example, a displacement having a margin of 10%. In other words, since the refractory expands when heated and contracts when the temperature decreases, the displacement is smaller than when the operation is stopped, but the refractory does not return completely due to the characteristics of the refractory, and heating and cooling are repeated. Over time, the displacement during heating increases, and the displacement gradually increases even when cooled. If the load applied to the frame constituting the furnace body 2, for example, the backstay 2a, exceeds the elastic limit for plastic deformation of the backstay 2a due to the displacement of the furnace body 2, the operating temperature is lowered. This is because the furnace body 2 remains in a deformed state.

操業温度を下げる制御として、原料混合制御部12は、精鉱と発熱量の小さい原料、例えば、酸化鉄スラグを混合する原料混合装置22において精鉱に供給する酸化鉄スラグの量を増加させ、装入量制御部13は、精鉱を装入する精鉱装入装置23の動作を制御して時間当たりの装入量を減少させ、冷却制御部14は、水冷ジャケット30内に供給する冷却水の水量及び/又は流速を増加させることで炉底部の冷却を促進し、還元材投入制御部15は、還元材投入装置24から炉内に投入される還元材の投入量を調整する。また、炉底部の冷却は、冷却制御部14によって炉底部に向かって冷風を吹き付ける図示しないファンの出力を制御することにより炉底部を冷却したり、炉内へ供給する反応ガスの酸素濃度を減少させて炉内温度の調整を行うように構成することもできる。尚、還元材の投入は炉体の複数箇所から行われるようになっており、例えば、温度の高いエリアへ投入する還元材の投入量を減らす、あるいは中止することで当該エリアの炉内壁に形成されるマグネタイト主体のセルフコーティングの厚みが増加するので当該エリアの炉内温度を部分的に下げることができる。また、所望金属が濃縮したマット層中の所望金属の品位、すなわち、マットグレード(MG)に基づいて管理を行うこともできる。例えば、MGを低くすることによって発熱量を減少させ、炉内操業温度を下げるという調整も可能である。   As control for lowering the operating temperature, the raw material mixing control unit 12 increases the amount of iron oxide slag supplied to the concentrate in the raw material mixing device 22 for mixing the concentrate and the raw material having a small calorific value, for example, iron oxide slag, The charging amount control unit 13 controls the operation of the concentrate charging device 23 for charging the concentrate to reduce the charging amount per hour, and the cooling control unit 14 cools the cooling water supplied into the water cooling jacket 30. Cooling of the bottom of the furnace is promoted by increasing the amount and / or flow rate of water, and the reducing material charging control unit 15 adjusts the amount of reducing material charged into the furnace from the reducing material charging device 24. In addition, the cooling of the bottom of the furnace is performed by controlling the output of a fan (not shown) that blows cool air toward the bottom of the furnace by the cooling control unit 14 to cool the bottom of the furnace or to reduce the oxygen concentration of the reaction gas supplied into the furnace. It is also possible to adjust the furnace temperature. The reducing material is introduced from a plurality of locations in the furnace body. For example, the amount of reducing material introduced into a high-temperature area is reduced or stopped to form on the furnace inner wall of the area. Since the thickness of the magnetite-based self-coating is increased, the furnace temperature in the area can be partially reduced. Further, the management can be performed based on the quality of the desired metal in the mat layer in which the desired metal is concentrated, that is, the mat grade (MG). For example, it is possible to adjust the heat generation amount to be decreased by lowering the MG and the operating temperature in the furnace is lowered.

[金属精練炉の操業方法]
次に、本発明に係る金属精錬炉の操業方法の一実施形態について説明する。図5は本発明に係る金属精練炉の操業方法の一実施形態のフローチャートである。まず、操業が開始されると、各変位計8−1〜8−42に対応する炉体2の各バックステイ2a,2aについて局所的な膨張に伴う変位がそれぞれ所定時間毎に計測され(ステップS1)、その計測値が演算部11に取り込まれる。演算部11は、各変位計8−1〜8−42の少なくとも一つ以上が予め設定した変位の上限値の範囲内か否かを監視する。そして、制御装置10の演算部11が少なくとも一つ以上の変位計8−1〜8−42が上限値を超えたと判断した場合(ステップS2:Yes)には、(A)原料混合制御部12が原料混合装置22の動作を制御して炉体2に装入する原料について発熱量の小さい原料の混合比率を増加する、(B)装入量制御部13が精鉱装入装置23の動作を制御して炉体2に装入する原料の時間当たりの装入量を下げる(例えば、210t/hから170t/hへ下げる)、(C)冷却制御部15は水冷ジャケット30の冷却水の水量を調整して炉体2の温度を下げる、(D)還元材投入制御部15が還元材投入装置24の動作を制御して炉体2内へ投入する還元材の量を減らす或いは中止することにより炉内壁へのセルフコーティングを促し、炉内コーティングを厚くする、(E)マット層中の所望金属のMGを下げること、のいずれか又は上記(A)〜(E)のいずれかの組み合わせによって操業温度を下げ(ステップS3)、変位量が上限以下となるように制御を行う。尚、還元材投入制御部15は、複数の還元材投入装置24の中で、温度の高いエリアに配置された還元材投入装置24についてのみ投入量を調整することにより部分的にセルフコーティングの厚みを制御することができる。
[Operation method of metal smelting furnace]
Next, an embodiment of a method for operating a metal refining furnace according to the present invention will be described. FIG. 5 is a flowchart of an embodiment of a method for operating a metal smelting furnace according to the present invention. First, when the operation is started, displacement associated with local expansion is measured for each backstay 2a, 2a of the furnace body 2 corresponding to each displacement meter 8 -1 to 8 -42 at predetermined time intervals (steps). S <b> 1), and the measurement value is taken into the calculation unit 11. The computing unit 11 monitors whether or not at least one of the displacement meters 8 −1 to 8 −42 is within the range of the preset upper limit value of displacement. When the calculating unit 11 of the control device 10 determines that at least one displacement gauge 8 -1 8 -42 exceeds the upper limit value: (step S2 Yes) is, (A) a raw material mixing control unit 12 Controls the operation of the raw material mixing device 22 and increases the mixing ratio of the raw material with a small calorific value for the raw material charged into the furnace body 2. (B) The charging amount control unit 13 operates the concentrate charging device 23. (C) The cooling control unit 15 lowers the amount of raw material charged into the furnace body 2 per hour (for example, from 210 t / h to 170 t / h). The temperature of the furnace body 2 is lowered by adjusting the amount of water. (D) The reducing material charging control unit 15 controls the operation of the reducing material charging device 24 to reduce or stop the amount of reducing material charged into the furnace body 2. Promotes self-coating on the inner wall of the furnace, The operating temperature is lowered by any one of (E) lowering the MG of the desired metal in the mat layer or any combination of the above (A) to (E) (step S3) Control is performed so as to be below the upper limit. The reducing material charging control unit 15 adjusts the charging amount only for the reducing material charging device 24 arranged in a high temperature area among the plurality of reducing material charging devices 24 to partially increase the self-coating thickness. Can be controlled.

このような制御により炉体2の変位を適正範囲に維持することができるので経年的に生じる炉長変化が監視できる結果、炉体2の塑性変形の範囲内で操業、即ち、炉体2の構成部材を破断させることなく管理することが可能となり、湯漏れや炉体構成部材の破断が発生する前に補強等の対策を実施することが可能となる。そして、湯漏れリスク低減や炉体寿命の延長を図ることが可能となる。また、局所的な膨張が観測された場合は、そのエリア付近での冷却を強化することで、その部分における湯漏れリスクを低減することも可能となる。   Since the displacement of the furnace body 2 can be maintained in an appropriate range by such control, the change in the furnace length that occurs over time can be monitored. As a result, the operation within the range of plastic deformation of the furnace body 2, that is, the furnace body 2 It becomes possible to manage the constituent members without breaking them, and it is possible to take measures such as reinforcement before the hot water leaks or the furnace body constituent members break. And it becomes possible to aim at the risk reduction of a hot water leak, and the extension of a furnace body lifetime. In addition, when local expansion is observed, it is possible to reduce the risk of hot water leakage in that portion by enhancing cooling in the vicinity of the area.

上述した制御によって各変位計8−1〜8−42の計測値が上限値以下となった場合(ステップS4:Yes)には、制御部10は、原料混合制御部12、装入量制御部13、冷却制御部14に対して予め設定された通常操業の動作を行うように指令を送り、操業温度が上限値以下である適正範囲内での操業を継続する(ステップS5)。一方、上述した制御によって各変位計8−1〜8−42の計測値が未だ上限値以下になっていない場合には(ステップS4:No)、ステップS3の処理を継続する。 When the measured values of the displacement meters 8 −1 to 8 −42 are equal to or lower than the upper limit values by the control described above (step S4: Yes), the control unit 10 includes the raw material mixing control unit 12 and the charging amount control unit. 13. A command is sent to the cooling control unit 14 so as to perform a preset normal operation, and the operation is continued within an appropriate range where the operation temperature is not more than the upper limit value (step S5). On the other hand, when the measured values of the displacement meters 8 -1 to 8-42 are not yet below the upper limit values (step S4: No), the process of step S3 is continued.

上述のような操業を継続することにより、各変位計8−1〜8−42の計測値によって算出される炉体2の残存線膨張率が所定に割合を超えた場合には炉体2を形成する各種炉材の更新を行う。ここで、上述したように、バックステイ2aに付加される荷重がバックステイ2aを塑性変形させる弾性限界を超えてしまうと炉体2を冷却してもその変位は元に戻ることがないため、各種炉材の更新の目安とする残存線膨張率については、少なくともバックステイ2aを塑性変形させる弾性限界を超えないような割合に設定することが好ましい。 By continuing the operation as described above, when the residual linear expansion coefficient of the furnace body 2 calculated by the measured values of the displacement meters 8 -1 to 8-42 exceeds a predetermined ratio, the furnace body 2 is Renew various furnace materials to be formed. Here, as described above, if the load applied to the backstay 2a exceeds the elastic limit for plastically deforming the backstay 2a, the displacement does not return to the original even if the furnace body 2 is cooled. It is preferable to set the residual linear expansion coefficient, which serves as a standard for renewal of various furnace materials, to a ratio that does not exceed at least the elastic limit for plastic deformation of the backstay 2a.

以上のように、本実施形態に係る金属精練炉の操業方法によれば、変位計8−1〜8−42によって炉体2の変位(膨張)、例えば、炉体2の側壁を支持する各バックステイ2aの変位を計測し、少なくとも一箇所以上の変位が予め設定した上限値を超えることとなったときに、上記変位が上限値以下となるように制御装置10によって炉体2内の操業温度を下げる、あるいは上限を超えたエリアのコーティング厚みを増加させて操業温度を下げるように構成したので、炉体2の膨張や変形を適正な範囲内に維持することができ、炉体2の熱膨張による炉底の耐火レンガの配列の崩れや、空隙の発生等を防止することが可能となる。 As described above, according to the operation method of the metal smelting furnace according to the present embodiment, the displacement (expansion) of the furnace body 2, for example, the side walls of the furnace body 2 are supported by the displacement meters 8 −1 to 8 -42 . When the displacement of the backstay 2a is measured and at least one displacement exceeds a preset upper limit value, the controller 10 operates the furnace body 2 so that the displacement becomes equal to or less than the upper limit value. Since the operation temperature is lowered by decreasing the temperature or increasing the coating thickness in the area exceeding the upper limit, the expansion and deformation of the furnace body 2 can be maintained within an appropriate range. It becomes possible to prevent the arrangement of the firebrick at the bottom of the furnace due to thermal expansion, the generation of voids, and the like.

また、本実施形態に係る金属精練炉の操業方法によれば、炉体2の周囲に所定間隔ごとに変位計8−1〜8−42によって炉体2の全体の変位を計測することとしたので、炉長変化を随時監視することができ、適切なタイミングで炉材を更新することが可能となる。 Further, according to the operating method of the metal refining furnace according to the present embodiment, it was decided to measure the entire displacement of the furnace body 2 by the displacement gauge 8 -1 8 -42 at predetermined intervals around the furnace body 2 Therefore, the furnace length change can be monitored at any time, and the furnace material can be updated at an appropriate timing.

さらに、本実施形態に係る金属精練炉の操業方法によれば、炉体の残存線膨張率が所定の割合を超えた場合に炉体を形成する各種炉材の更新を行うことにより、大事に至る前に更新が行えるため、操業停止を短くし、且つ修理費を低減できるという効果がある。   Furthermore, according to the operation method of the metal smelting furnace according to the present embodiment, by updating the various furnace materials forming the furnace body when the residual linear expansion coefficient of the furnace body exceeds a predetermined ratio, Since renewal can be performed before the end, there is an effect that operation stoppage can be shortened and repair costs can be reduced.

[他の実施の形態]
本発明は、上記各実施例に限定されるものではなく、本発明の技術思想を逸脱あるいは変更しない範囲内で種々な変形が可能であることはいうまでもない。
[Other embodiments]
The present invention is not limited to the above embodiments, and it goes without saying that various modifications can be made without departing from or changing the technical idea of the present invention.

1 金属精練炉
2 炉体
2a バックステイ
3 反応シャフト
4 アップテイク
5 セットラ
6 精鉱バーナ
7 予熱空気注入口
8 変位計
10 制御装置
11 演算部
12 原料混合制御部
13 装入量制御部
14 冷却制御部
15 還元材投入制御部
22 原料混合装置
23 精鉱装入装置
24 還元材投入装置
30 水冷ジャケット
DESCRIPTION OF SYMBOLS 1 Metal smelting furnace 2 Furnace body 2a Backstay 3 Reaction shaft 4 Uptake 5 Settler 6 Concentration burner 7 Preheating air inlet 8 Displacement meter 10 Control apparatus 11 Calculation part 12 Raw material mixing control part 13 Charge amount control part 14 Cooling control 15 Reducing material charging control unit 22 Raw material mixing device 23 Concentrate charging device 24 Reducing material charging device 30 Water cooling jacket

Claims (6)

炉体の膨張や変形を所定の範囲内に維持する金属精錬炉の操業方法において、
複数の変位計によって前記炉体の所定の複数箇所の変位をそれぞれ計測し、少なくとも一箇所以上の変位が予め設定した上限値を超えることとなった場合には、当該変位が前記上限値以下となるように前記炉体内の操業温度を下げることを特徴とする金属精錬炉の操業方法。
In the method of operating a metal refining furnace that maintains expansion and deformation of the furnace body within a predetermined range,
When a plurality of displacement gauges measure a plurality of displacements at a predetermined location of the furnace body and at least one displacement exceeds a preset upper limit value, the displacement is equal to or less than the upper limit value. A method for operating a metal refining furnace, characterized in that the operating temperature in the furnace body is lowered.
請求項1に記載の金属精錬炉の操業方法において、
前記変位が予め設定した上限値を超えることとなった場合には、
A.前記炉体に装入する原料について発熱量の小さい原料の混合比率を増加すること、
B.前記炉体に装入する原料の時間当たりの装入量を減らすこと、
C.前記炉体の冷却を行うこと、
D.還元材の投入量を調整することによりセルフコーティングを形成しやすい炉内環境とすること、
E.マット層中の銅品位(マットグレード(MG))を下げること、
のいずれか又はA乃至Eのいずれかの組み合わせによって前記炉体内の操業温度を下げることを特徴とする金属精錬炉の操業方法。
In the operation method of the metal smelting furnace according to claim 1,
When the displacement exceeds the preset upper limit value,
A. Increasing the mixing ratio of raw materials with small calorific values for the raw materials charged into the furnace body;
B. Reducing the amount of raw material charged into the furnace body per hour;
C. Cooling the furnace body;
D. By adjusting the amount of reducing material input, make the furnace environment easy to form a self-coating,
E. Lowering the copper grade (mat grade (MG)) in the mat layer,
A method for operating a metal refining furnace, wherein the operating temperature in the furnace body is lowered by any one of the above or a combination of any of A to E.
請求項1又は2に記載の金属精錬炉の操業方法において、
前記変位計は、前記炉体の周囲に所定間隔ごとに配置し、前記炉体の全体の変位を計測することを特徴とする金属精錬炉の操業方法。
In the operation method of the metal smelting furnace according to claim 1 or 2,
The displacement meter is arranged at predetermined intervals around the furnace body, and measures the total displacement of the furnace body.
請求項3項に記載の金属精錬炉の操業方法において、
前記変位計は、前記炉体の側壁を支持する各バックステイの変位を計測することを特徴とする金属精錬炉の操業方法。
In the operation method of the metal smelting furnace according to claim 3,
The method for operating a metal refining furnace, wherein the displacement meter measures a displacement of each backstay that supports a side wall of the furnace body.
請求項1から4のいずれか1項に記載の金属精錬炉の操業方法において、
前記上限値は、前記炉体が変位することによって当該炉体を構成するフレームに付加される荷重が当該フレームを塑性変形させる弾性限界を超えない変位であることを特徴とする金属精錬炉の操業方法。
In the operation method of the metal smelting furnace according to any one of claims 1 to 4,
The upper limit value is a displacement in which a load applied to a frame constituting the furnace body due to the displacement of the furnace body does not exceed an elastic limit for plastically deforming the frame. Method.
請求項1から5のいずれか1項に記載の金属精錬炉の操業方法において、
前記変位計の計測値によって算出される前記炉体の残存線膨張率が所定の割合を超えた場合に前記炉体を形成する各種炉材の更新を行うことを特徴とする金属精錬炉の操業方法。
In the operation method of the metal smelting furnace according to any one of claims 1 to 5,
An operation of a metal smelting furnace characterized in that when a residual linear expansion coefficient of the furnace body calculated by a measured value of the displacement meter exceeds a predetermined ratio, various furnace materials forming the furnace body are updated. Method.
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