JPS61291890A - Drying temperature-elevation method of vessel for molten metal - Google Patents

Drying temperature-elevation method of vessel for molten metal

Info

Publication number
JPS61291890A
JPS61291890A JP13258585A JP13258585A JPS61291890A JP S61291890 A JPS61291890 A JP S61291890A JP 13258585 A JP13258585 A JP 13258585A JP 13258585 A JP13258585 A JP 13258585A JP S61291890 A JPS61291890 A JP S61291890A
Authority
JP
Japan
Prior art keywords
container
air
drying
temperature
molten metal
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.)
Granted
Application number
JP13258585A
Other languages
Japanese (ja)
Other versions
JPS6354996B2 (en
Inventor
孝夫 鈴木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP13258585A priority Critical patent/JPS61291890A/en
Publication of JPS61291890A publication Critical patent/JPS61291890A/en
Publication of JPS6354996B2 publication Critical patent/JPS6354996B2/ja
Granted legal-status Critical Current

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Landscapes

  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Furnace Housings, Linings, Walls, And Ceilings (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は製銑、製鋼で使用される混銑車、取鍋等の溶融
金属用容器の乾燥昇温方法に関するもので、特にカーボ
ン、グラファイト、炭化珪素またはSi3N4等の易酸
化性耐火物を内張すした容器の寿命延長を可能とする安
価な乾燥昇温方法を提供するものである。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method for drying and heating up containers for molten metal such as pig iron mixers and ladles used in pig iron making and steel making. The object of the present invention is to provide an inexpensive drying and temperature raising method that allows extending the life of containers lined with easily oxidizable refractories such as silicon carbide or Si3N4.

〔従来の技術〕[Conventional technology]

従来の溶融金属用容器の乾燥昇温の多くは手動にて行わ
れていた。このため乾燥用空気量と燃料との比(空燃比
)の調節は、操業者のカンに頼っており、容器内の残留
02量は常に不安定であった。この残留02量は、従来
のようなシャモット系の酸化性耐火物を内張すした容器
においては、その影響は小さく、さして問題とならなか
った。
In the past, most of the drying and heating of molten metal containers was done manually. For this reason, the adjustment of the ratio of the amount of drying air to the fuel (air-fuel ratio) was dependent on the operator's control, and the amount of O2 remaining in the container was always unstable. This residual amount of 02 had a small effect on conventional containers lined with chamotte-based oxidizing refractories and did not pose much of a problem.

しかし近年高品質鋼の生産を目的として容器内で各種の
処理、例えば混銑車での脱S、脱Si、脱Pまたは取鍋
での脱S等が行われるようになり、その容器の耐用向上
のために、カーボン、グラファイト、炭化珪素などの易
酸化性耐火物を内張すすることが頻繁に実施されるよう
になってきた。易酸化性耐火物は緻密性がよく、スラグ
と接した時には非常に濡れに〈<、鉄酸化物を還元し強
固なコーティング層を形成する等、酸化性耐火物に比べ
て非常に優れた耐食性を有している。
However, in recent years, for the purpose of producing high-quality steel, various treatments have been carried out inside the container, such as de-S, de-Si, de-P in a pig iron mixer, de-P in a ladle, etc., and the durability of the container has improved. For this reason, lining with easily oxidizable refractories such as carbon, graphite, and silicon carbide has become a frequent practice. Easily oxidizable refractories have good density, and when they come into contact with slag, they become very wet. have.

反面、この易酸化性耐火物は、高温時において容器内の
02m度が高いと表面が容易に酸化反応し、ボロボロに
なって剥離してしまう欠点を有している。この対策とし
て乾燥昇温を自動化し、一定した低空燃比で燃焼を行わ
せる、すなわち流量による空燃比制御が行われているが
、低温時において低空燃比で燃焼を行うことは、乾燥用
バーナの噴出力を減じ、容器内の燃焼ガスの攪拌や循環
が十分でなく、乾燥時間を延長せざるを得す、長時間を
要した。
On the other hand, this easily oxidizable refractory has the disadvantage that when the temperature inside the container is high, the surface easily undergoes an oxidation reaction, becomes crumbly and peels off. As a countermeasure to this problem, the drying temperature rise is automated and combustion is performed at a constant low air-fuel ratio, that is, the air-fuel ratio is controlled by flow rate. The drying time was forced to be extended due to reduced power, insufficient stirring and circulation of the combustion gas in the container, and a longer drying time.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明は上記の点に鑑みて発明されたもので、易酸化性
耐火物の乾燥昇温において、容器内の02との酸化反応
の少ない低温時においては、高空燃比で燃焼を行い、容
器内の燃焼ガスの攪拌と循環性を高め、乾燥時間の短縮
を図る。そして、酸化反応の影響の大きい高温時におい
ては、低空燃比で燃焼する溶融金属用乾燥昇温方法を提
供することを目的としている。
The present invention was invented in view of the above points, and when drying and heating easily oxidizable refractories, combustion is performed at a high air-fuel ratio at low temperatures where there is little oxidation reaction with 02 in the container. Improves the agitation and circulation of combustion gas and shortens drying time. Another object of the present invention is to provide a method for drying and heating molten metal that burns at a low air-fuel ratio at high temperatures where the influence of oxidation reactions is large.

〔問題点を解決するための手段〕[Means for solving problems]

上記の目的達成のため、乾燥昇温をあらかじめ設定され
た昇温パターンに従って自動的に昇温させると共に、昇
温パターンの低温度域では高空燃比にて燃焼を行う比率
設定を行い、高温域時には低空燃比にて燃焼を行う比率
設定を行い、この比率設定の切り替えを容器内の温度測
定によって行う溶融金属用容器の乾燥昇温方法によって
目的を達成するものである。
In order to achieve the above objectives, the drying temperature is automatically raised according to a preset heating pattern, and the ratio is set to perform combustion at a high air-fuel ratio in the low temperature range of the heating pattern, and in the high temperature range. This objective is achieved by a method for drying and heating a container for molten metal, in which a ratio is set to perform combustion at a low air-fuel ratio, and the ratio setting is switched by measuring the temperature inside the container.

〔作用〕[Effect]

次に本発明を添付図に基づいて作用とともに説明する。 Next, the present invention will be explained along with its operation based on the accompanying drawings.

第2図、第3図はそれぞれ本発明方法を実施した混銑車
および取鍋の乾燥装置であり、第2図において1は易酸
化性物質を含有する耐火物で内張りされた溶融金属用容
器である混銑車、2.2aは混銑車乾燥用高速燃焼バー
ナ、3はバーナを前後に移動させるレール、4は架台で
ある。第3図において5は取鍋で易酸化性物質を含有す
る耐火物で内張すされ工おり、6は取鍋乾燥用高速バー
ナ、7はバーナを備えた取着、8は取着開閉装置である
Figures 2 and 3 show a pig iron mixer car and a ladle drying device, respectively, in which the method of the present invention was carried out, and in Figure 2, 1 is a container for molten metal lined with a refractory material containing easily oxidizable substances. In a certain pig iron mixer car, 2.2a is a high-speed combustion burner for drying the pig iron mixer car, 3 is a rail for moving the burner back and forth, and 4 is a frame. In Figure 3, 5 is a ladle lined with a refractory material containing easily oxidizable substances, 6 is a high-speed burner for drying the ladle, 7 is a mounting equipped with a burner, and 8 is a mounting opening/closing device. It is.

第1図は本発明方法の制御系統図の1例であって、溶融
金属容器1または5を乾燥昇温する。9はバーナ、10
は容器内の温度を検知する熱電対、11はあらかじめ設
定された昇温パターンに従って自動的に昇温するための
プログラム昇温制御器であり、昇温パターンに従って燃
料および空気量の供給量を調節する。12は低温時用の
空燃比設定器、13は高温用の空燃比設定器、14は切
替スイッチ、15は燃料配管、16は燃焼用空気配管、
17は燃焼空気ブロワ、18は燃料流量調節弁、19は
燃料空気流量調節弁である。なお、第1図では空燃比設
定器12.13は2個を備え切替スイッチで切り替えて
いるが、シーケンスを組み1個とすることができる。
FIG. 1 is an example of a control system diagram of the method of the present invention, in which a molten metal container 1 or 5 is heated to dry. 9 is burner, 10
11 is a thermocouple that detects the temperature inside the container, and 11 is a program temperature increase controller that automatically increases the temperature according to a preset temperature increase pattern, and adjusts the amount of fuel and air supplied according to the temperature increase pattern. do. 12 is an air-fuel ratio setting device for low temperatures, 13 is an air-fuel ratio setting device for high temperatures, 14 is a changeover switch, 15 is a fuel pipe, 16 is a combustion air pipe,
17 is a combustion air blower, 18 is a fuel flow rate control valve, and 19 is a fuel air flow rate control valve. In FIG. 1, two air-fuel ratio setting devices 12 and 13 are provided and switched by a changeover switch, but they can be set to one by setting a sequence.

次に、本発明方法の作動に?いてコークス炉ガスを燃料
として混銑車を乾燥する場合について説明する。まず、
混銑車1内に混銑車バーナ2が挿入され、プログラム昇
温制御器11によって決めたれた昇温カーブに沿って乾
燥が開始される。この際、切替スイッチ14は、低温用
空燃比設定器12が作動するようになっており、その比
率は、空燃比R/B=1.5となるようにセットされて
いる。昇温時(昇温プログラムパターン)の燃焼負荷に
応じて燃料流量調節弁18の開度が自動制御される。こ
れに合わせて燃焼空気流量調節弁19の開度は設定され
た空気比になるよう制御され、いかなる燃焼負荷におい
ても空燃比R/B=1.5倍の流量が得られるようにな
っている。
Next, what about the operation of the method of the present invention? The following describes the case where a pig iron mixer car is dried using coke oven gas as fuel. first,
The pig iron mixer burner 2 is inserted into the pig iron mixer 1, and drying is started along a temperature rise curve determined by the programmed temperature rise controller 11. At this time, the changeover switch 14 is configured to operate the low temperature air-fuel ratio setter 12, and the ratio is set so that the air-fuel ratio R/B=1.5. The opening degree of the fuel flow control valve 18 is automatically controlled according to the combustion load during temperature rise (temperature increase program pattern). In accordance with this, the opening degree of the combustion air flow rate control valve 19 is controlled to reach the set air ratio, so that a flow rate of air-fuel ratio R/B = 1.5 times can be obtained under any combustion load. .

次に、この状態であらかじめ設定されたパターンにより
600℃まで昇温を行う、熱電対10によって測定され
た温度が600℃を超えるとプログラム昇温制御器11
より信号が発せられ、切替スイッチ14が作動し、低温
時用比率設定器12から高温時用比率設定器13に切替
える。この際、その比率は空燃比R/B=1.0となる
ようにセットされている。これに伴って燃焼空気用バル
ブ19の開度は常に最低空気量(R/B=lO)のみが
得られるように変更される。以降、乾燥終了までこの状
態が持続され、昇温パターンに従って昇温される。
Next, in this state, the temperature is raised to 600°C according to a preset pattern. When the temperature measured by the thermocouple 10 exceeds 600°C, the program temperature increase controller 11
A signal is issued, the changeover switch 14 is activated, and the low temperature ratio setting device 12 is switched to the high temperature ratio setting device 13. At this time, the ratio is set so that the air-fuel ratio R/B=1.0. Accordingly, the opening degree of the combustion air valve 19 is changed so that only the minimum amount of air (R/B=lO) is always obtained. Thereafter, this state is maintained until the end of drying, and the temperature is increased according to the temperature increase pattern.

なお、低温域から高温域への空燃比の切り替え設定温度
について説明する。
Note that the set temperature for switching the air-fuel ratio from the low temperature range to the high temperature range will be explained.

本発明者らの実験によれば、第4図に示すように容器内
酸素濃度が上昇するにつれて酸化消失深さが増大するが
、容器内温度が600℃を超えると、急激に酸化消失が
大きくなる。従って高温でかつ02濃度が高くなれば耐
火物中のCの酸化が著しく800℃前後でバーナの燃焼
を低空気燃焼とする必要がある。
According to experiments conducted by the present inventors, as shown in Figure 4, the depth of oxidation loss increases as the oxygen concentration inside the container increases, but when the temperature inside the container exceeds 600°C, the oxidation loss suddenly increases. Become. Therefore, if the temperature is high and the O2 concentration is high, the oxidation of C in the refractory will be significant, and at around 800° C., it is necessary to perform low air combustion in the burner.

〔実施例〕〔Example〕

実施例1 混銑車での乾燥昇熱を行った。 Example 1 Dry heating was carried out in a pig iron mixing car.

容器内張りとして A文203:63重量% 5t02:15!を量% SiC:10重量% 黒鉛:10重量% のれんかを全面にライニングした混銑車において、旧来
の操業者の感に頼る方法(昇温開始から完了まで空燃比
的R/B=1.5)による乾燥昇熱と本発明による乾燥
昇熱を行った混銑車の寿命と脱S処理比率との関係を第
5図に示す0本発明によって、従来方式より50〜10
0ヒート寿命が向上した結果を得た。
As a container lining A text 203:63% by weight 5t02:15! Amount% SiC: 10% by weight Graphite: 10% by weight In a mixed pig iron car completely lined with bricks, the traditional method of relying on the operator's intuition (air-fuel ratio R/B = 1.5 from the start of heating to the completion) ) The relationship between the life of the pig iron mixer car and the S removal treatment ratio is shown in Figure 5.
The result was that the 0-heat life was improved.

この寿命向上は、先の予備テストでの酸化消失層の厚み
に対応している。
This improvement in life corresponds to the thickness of the oxidation dissipation layer in the previous preliminary test.

実施例2 実施例1と同様な装置による乾燥昇熱をスラグラインに
マグネシアカーボン(15重量%)れんがをライニング
した取鍋において試験した。その結果は、第6図に示す
ように、旧来方式(昇温開始から完了まで空燃比R/B
=1.5)に比べて本発明による乾燥昇熱によって、同
−溶鋼脱S処理比率において約lOヒートの寿命向上を
得た。
Example 2 Dry heating with equipment similar to Example 1 was tested in a ladle lined with magnesia carbon (15% by weight) bricks in the slag line. As shown in Figure 6, the results are as follows:
= 1.5), the dry heating according to the present invention resulted in an improvement in life of about 10 heat at the same molten steel desulfurization treatment ratio.

〔発明の効果〕〔Effect of the invention〕

本発明の方法により、次のような効果を得た。 By the method of the present invention, the following effects were obtained.

上記実施例1.2に示したように、旧来の操業者の感に
頼る方法に比し容器の寿命が向上した。
As shown in Example 1.2 above, the life of the container was improved compared to the conventional method relying on operator intuition.

また、第7rgJに示すように昇温開始から酸化防止の
ため低空燃比で行う従来昇温に比べ高速燃焼バーナによ
り低温時における高空燃比燃焼によって、大きなバーナ
の噴出力が得られ、容器内の燃焼ガスを攪拌、循環でき
、かつ600℃の高温時での低空燃比に切替えることに
よって無駄な熱ロスがなくなり、乾燥昇温時間およびエ
ネルギーを大幅に改善できた。また、耐火物の寿命も従
来の乾燥昇温に比べ約20%向上させることができた。
In addition, as shown in No. 7 rgJ, compared to the conventional temperature raising that is performed at a low air-fuel ratio from the start of temperature raising to prevent oxidation, the high-speed combustion burner performs combustion at a high air-fuel ratio at low temperatures, resulting in a large burner injection force, which increases the combustion inside the container. By being able to stir and circulate the gas and switching to a low air-fuel ratio at a high temperature of 600°C, wasted heat loss was eliminated, and drying heating time and energy were significantly improved. Furthermore, the lifespan of refractories was improved by about 20% compared to conventional drying and temperature raising methods.

【図面の簡単な説明】 第1図は本発明方法を示す制御系統図、第2図、第3図
はそれぞれ本発明方法を実施した混銑車および取鍋の乾
燥加熱装置、第4図は容器内の酸素濃度と酸化消失深さ
との関係を示すグラフ、第5図、第6rI!Iは本発明
方法と従来方法による耐火物の寿命を比較したグラフ、
第7図は乾燥温度パターンの例を示すグラフである。 ■・・・混銑車      2,6.9・・・バーナ3
・・・レール      4・・・架台5・・・取鍋 
      7・・・取着8・・・板蓋開閉装置i1 
  10・・・熱電対11・・・プログラム昇温制御器 12.13・・・空燃比設定器 14・・・切替スイッチ  15・・・燃料配管16・
・・空気配管    17・・・ブロワ18.19・・
・調節弁
[Brief Description of the Drawings] Fig. 1 is a control system diagram showing the method of the present invention, Figs. 2 and 3 are drying and heating devices for a pig iron mixer car and a ladle, respectively, in which the method of the present invention was implemented, and Fig. 4 is a container Graphs showing the relationship between oxygen concentration and oxidation loss depth in Figures 5 and 6rI! I is a graph comparing the life of refractories according to the method of the present invention and the conventional method,
FIG. 7 is a graph showing an example of a drying temperature pattern. ■・・・Pigtail car 2, 6.9...Burner 3
...Rail 4 ... Frame 5 ... Ladle
7...Installation 8...Plate lid opening/closing device i1
10...Thermocouple 11...Program temperature increase controller 12.13...Air-fuel ratio setter 14...Selector switch 15...Fuel pipe 16.
...Air piping 17...Blower 18.19...
·Control valve

Claims (1)

【特許請求の範囲】 1 易酸化性質物を含有する耐火物で内張りされた溶融
金属用容器を乾燥昇温するにあた り、前記容器を、容器内温度を測定しなが ら、あらかじめ設定された昇温パターンに 従って乾燥昇温させるとともに、昇温パターンの低温度
域ではバーナの燃焼を高空燃比にて行い、高温域では低
空燃比に切り替えて バーナ燃焼を行うことを特徴とする溶融金属用容器の乾
燥昇温方法。
[Claims] 1. When drying and heating a molten metal container lined with a refractory material containing an easily oxidizable material, the container is heated in a preset heating pattern while measuring the internal temperature of the container. Drying and temperature raising of a container for molten metal, which is characterized by drying and heating a container for molten metal, and performing burner combustion at a high air-fuel ratio in the low temperature range of the temperature rising pattern, and switching to a low air-fuel ratio and performing burner combustion in the high temperature range. Method.
JP13258585A 1985-06-18 1985-06-18 Drying temperature-elevation method of vessel for molten metal Granted JPS61291890A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13258585A JPS61291890A (en) 1985-06-18 1985-06-18 Drying temperature-elevation method of vessel for molten metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13258585A JPS61291890A (en) 1985-06-18 1985-06-18 Drying temperature-elevation method of vessel for molten metal

Publications (2)

Publication Number Publication Date
JPS61291890A true JPS61291890A (en) 1986-12-22
JPS6354996B2 JPS6354996B2 (en) 1988-10-31

Family

ID=15084775

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13258585A Granted JPS61291890A (en) 1985-06-18 1985-06-18 Drying temperature-elevation method of vessel for molten metal

Country Status (1)

Country Link
JP (1) JPS61291890A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02183793A (en) * 1989-01-09 1990-07-18 Nippon Steel Corp Drying control method and device for ladle
WO2018135024A1 (en) * 2017-01-23 2018-07-26 中外炉工業株式会社 Heating device and heating method for interior of refractory material containers

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS503030A (en) * 1973-05-16 1975-01-13

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS503030A (en) * 1973-05-16 1975-01-13

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02183793A (en) * 1989-01-09 1990-07-18 Nippon Steel Corp Drying control method and device for ladle
WO2018135024A1 (en) * 2017-01-23 2018-07-26 中外炉工業株式会社 Heating device and heating method for interior of refractory material containers

Also Published As

Publication number Publication date
JPS6354996B2 (en) 1988-10-31

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