JPS6146751B2 - - Google Patents
Info
- Publication number
- JPS6146751B2 JPS6146751B2 JP17238081A JP17238081A JPS6146751B2 JP S6146751 B2 JPS6146751 B2 JP S6146751B2 JP 17238081 A JP17238081 A JP 17238081A JP 17238081 A JP17238081 A JP 17238081A JP S6146751 B2 JPS6146751 B2 JP S6146751B2
- Authority
- JP
- Japan
- Prior art keywords
- scrap
- preheating
- temperature
- exhaust gas
- solid fuel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000004449 solid propellant Substances 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 22
- 238000002844 melting Methods 0.000 claims description 20
- 230000008018 melting Effects 0.000 claims description 20
- 238000009628 steelmaking Methods 0.000 claims description 4
- 239000003610 charcoal Substances 0.000 description 13
- 238000002485 combustion reaction Methods 0.000 description 11
- 239000003245 coal Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 239000000446 fuel Substances 0.000 description 8
- 229910000831 Steel Inorganic materials 0.000 description 5
- 239000010959 steel Substances 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 238000009529 body temperature measurement Methods 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229910000975 Carbon steel Inorganic materials 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000010962 carbon steel Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000010309 melting process Methods 0.000 description 2
- 239000002436 steel type Substances 0.000 description 2
- 241001248531 Euchloe <genus> Species 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Furnace Details (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
本発明は製鋼用スクラツプ(以下単にスクラツ
プという)の予熱方法に関する。
鉄鋼の圧延加工等の際に供出されるスクラツプ
利用の一環として、スクラツプを電気炉等の溶解
炉で溶解せしめ、次いで特殊鋼等に製品化するこ
とが行われている。この溶解炉を使用してスクラ
ツプを溶解するに、スクラツプを予じめ予熱装置
を使用して予熱しておくことは、溶解炉で消費さ
れる熱エネルギーも少なくて済み省エネルギーと
いう観点からは好ましいことであるばかりでな
く、その溶解に要する時間も少なくて済む。又こ
の際の予熱方法として、溶解炉から排出される排
ガスの熱量を有効に利用しようという観点から、
溶解炉で発生した排ガスを予熱装置内に導入して
スクラツプを予熱することも行われている。
ここで、従来行われている排ガス利用によるス
クラツプの予熱方法について第1図に示すスクラ
ツプ予熱装置系統図を参照しつつ説明する。
第1図に於いて、符号1がスクラツプを溶解す
る溶解炉である。この溶解炉で発生した高温の排
ガスを燃焼塔4及びダクト5,6を経由して、ス
クラツプを装入した予熱装置7に導入して当該ス
クラツプを予熱する。尚第1図中符号8,9はダ
クトであり予熱に使用された排ガス等を次工程へ
導く通路である。予熱されたスクラツプは予熱装
置を移動せしめて溶解炉に投入され溶解工程に付
される。斯様なスクラツプの予熱(工程)におい
て、スクラツプの予熱温度を僅かでも上昇させる
ことは、スクラツプの溶解工程における電力消費
の節減等に大きく寄与するものであり、例えばス
クラツプ自体の温度で10℃程度の温度上昇でも溶
解時間が短縮され又電力消費は格段に少なくて済
む。この予熱スクラツプの温度を上昇せしめる為
には予熱装置内での予熱効果を高め当該装置内の
排ガス雰囲気温度を上昇せしめることが必要であ
る。しかるに従来法によれば予熱装置内の排ガス
雰囲気温度はせいぜい600〜650℃程度に留まり、
勢いスクラツプ自体の温度も低いものであつた。
排ガス利用によるスクラツプの予熱方法は前記
した通り有効な方法ではあるが、排ガスをそのま
ま予熱装置内に導入する方法では限界がある。そ
こでスクラツプの予熱温度をさらに上昇させる目
的で、プロパンガス等の気体燃料や、重油等の液
体燃料を使用するスクラツプ予熱装置も検討され
たが、これらはいづれもバーナその他の燃焼装置
を設ける必要があり、設備費が高くなるほか、こ
れらの燃料自体も高価なため経済的ではない。
本発明は、上述の従来法の有する欠点を解消し
た排ガスによるスクラツプの予熱方法を提供する
ものであり、溶解炉から排出される高温の排ガス
を用いてスクラツプを予熱するスクラツプの予熱
方法に於いて、スクラツプに固体燃料を添加し、
この固体燃料を排ガスにより燃焼させて予熱を行
うことを特徴とするスクラツプの予熱方法に存す
る。
本発明は、特別な設備改造を必要とせず、安価
な固体燃料を従来のスクラツプ予熱装置内に装入
しておくのみで、著しく予熱効果を高めることが
できる極めて経済的なスクラツプの予熱方法であ
る。
本発明に使用される固体燃料としては、オガラ
イト(商品名)で例示される木屑(おがくず等)
を圧縮固化して成る燃料、豆炭、コークス、木
炭、石炭、木、紙、タイヤ等が挙げられるが予熱
に用いられる排ガス温度、予熱時間、スクラツプ
量等に応じて適当なものが選択される。
スクラツプ予熱を行なうに際しては、限られた
時間内に最大の予熱効果を上げることが望まし
い。しかしその条件を満足させる燃料としては燃
焼熱量が高いと同時に燃焼速度が速いことが必要
となる。この様な条件を満足するものとして、オ
ガライトや豆炭の様な微粒子を圧着させたもの、
または、木炭の様にポーラスで燃焼表面積の大き
いものが良いことが実証された。また、燃料の着
火温度も低温であることを必要とするが、この点
石炭、コークスに比べて、オガライト、木炭、豆
炭等が優れる。さらにスクラツプの予熱効果を高
める要素として、発炎性の燃料が望ましいことが
解つた。即ちオガライト、木、等は、強力な炎を
発生して、クラムシエル内のスクラツプ全体を加
熱できる。
次の第1表は上記で例示した固体燃料について
その燃焼熱量と着火温度と燃焼速度を対比して示
したものである。
The present invention relates to a method for preheating steelmaking scrap (hereinafter simply referred to as scrap). BACKGROUND ART As part of the utilization of scrap provided during steel rolling processing, etc., the scrap is melted in a melting furnace such as an electric furnace, and then manufactured into products such as special steel. Before melting scrap using this melting furnace, it is preferable to preheat the scrap using a preheating device in advance, since the thermal energy consumed in the melting furnace is also small, which is preferable from the perspective of energy saving. Not only that, but the time required for its dissolution is also reduced. In addition, as a preheating method at this time, from the viewpoint of effectively utilizing the amount of heat of the exhaust gas discharged from the melting furnace,
Scrap is also preheated by introducing the exhaust gas generated in the melting furnace into a preheating device. Here, a conventional method of preheating scrap using exhaust gas will be explained with reference to a system diagram of a scrap preheating apparatus shown in FIG. In FIG. 1, reference numeral 1 is a melting furnace for melting scrap. The high-temperature exhaust gas generated in the melting furnace is introduced via the combustion tower 4 and ducts 5 and 6 into a preheating device 7 loaded with scrap to preheat the scrap. Note that reference numerals 8 and 9 in FIG. 1 are ducts, which are passages for guiding the exhaust gas used for preheating to the next process. The preheated scrap is moved from the preheating device and placed in the melting furnace, where it is subjected to the melting process. In such a scrap preheating (process), increasing the scrap preheating temperature even slightly will greatly contribute to reducing power consumption in the scrap melting process. For example, the temperature of the scrap itself can be increased by about 10 degrees Celsius. The melting time can be shortened even with a temperature increase of 500 mL, and power consumption can be significantly reduced. In order to raise the temperature of this preheating scrap, it is necessary to enhance the preheating effect within the preheating device and raise the temperature of the exhaust gas atmosphere within the device. However, according to the conventional method, the temperature of the exhaust gas atmosphere inside the preheating device remains at about 600 to 650°C,
The temperature of the momentum scrap itself was also low. Although the method of preheating scrap using exhaust gas is an effective method as described above, there are limits to the method of directly introducing the exhaust gas into the preheating device. Therefore, in order to further increase the preheating temperature of scrap, scrap preheating devices that use gaseous fuel such as propane gas or liquid fuel such as heavy oil have been considered, but all of these require the installation of a burner or other combustion device. However, in addition to high equipment costs, these fuels themselves are also expensive, making them uneconomical. The present invention provides a method for preheating scrap using exhaust gas that eliminates the drawbacks of the conventional method described above. , adding solid fuel to the scrap,
The present invention resides in a scrap preheating method characterized by preheating the solid fuel by burning it with exhaust gas. The present invention is an extremely economical scrap preheating method that does not require any special equipment modification and can significantly improve the preheating effect by simply charging an inexpensive solid fuel into a conventional scrap preheating device. be. The solid fuel used in the present invention includes wood chips (sawdust, etc.) exemplified by Ogalite (trade name).
Examples include fuel obtained by compressing and solidifying charcoal, coke, charcoal, coal, wood, paper, tires, etc., but an appropriate one is selected depending on the temperature of the exhaust gas used for preheating, the preheating time, the amount of scrap, etc. When performing scrap preheating, it is desirable to maximize the preheating effect within a limited time. However, a fuel that satisfies these conditions must have a high combustion heat and a high combustion rate. Products that satisfy these conditions include those made by compressing fine particles such as ogalite and charcoal,
Alternatively, it has been demonstrated that something porous and with a large burning surface area, such as charcoal, is better. Furthermore, the ignition temperature of the fuel needs to be low, and in this respect, ogalite, charcoal, pea charcoal, etc. are superior to coal and coke. Furthermore, it has been found that flammable fuel is desirable as an element to enhance the preheating effect of scrap. That is, ogalite, wood, etc. can produce a powerful flame that heats the entire scrap inside the clamshell. Table 1 below compares the combustion heat amount, ignition temperature, and combustion speed of the solid fuels exemplified above.
【表】【table】
【表】
示してある。
尚上記第1表中タイヤについては着火温度を示
していないが、タイヤは200℃位から溶解分解が
起きガス化し、当該ガスは炭化水素が主体となつ
ているので、その着火温度は500℃前後と推定さ
れる。従つて前記した事項及び上記第1表のデー
タ等から見て本発明の固体燃料としてはオガライ
トや豆炭の如き木屑等を粘結剤を使用して又は使
用せずに加熱圧縮して又は圧縮せずに固形化した
表面積の大きい固体燃料を使用することが好まし
い。就中オガライトは比較的低温で着火し(200
〜300℃)、急速に燃焼し、又着火後の温度は予熱
装置のクラムシエル上部で1000〜1100℃に達し燃
焼塔の排ガス温度より高くなる。又予熱し難いス
クラツプといえども赤熱する程に予熱効果を高
め、白煙も少ない。
上記固体燃料は1種又は2種以上が使用され
る。2種以上を併用して使用するときはより一層
予熱効果を高めることができる。例えばオガライ
トと石炭との併用を例として説明すると、予熱時
オガライトは早期に着火しその炎が石炭に当り、
燃焼熱量は高いが着火し難い石炭を着火し燃焼さ
せる。これにより石炭の予熱燃料としてのより一
層の有効利用を図ることができる。
本発明の予熱方法は予熱装置内にスクラツプを
装入するとともに固体燃料を当該スクラツプに添
加しておき、これに溶解炉から排出される高温の
排ガスを導入し、固体燃料を排ガス温度を利用し
て燃焼せしめスクラツプを予熱する。本発明のこ
の方法によれば排ガスの熱量と固体燃料の熱量と
が相俟つて予想以上に予熱装置内のガス雰囲気温
度を高め且スクラツプ温度を高めることができ
る。
第2図は本発明の予熱方法及びそれに使用され
る予熱装置の実施態様を示してある。第2図中1
0がスクラツプ、11が固体燃料、12がクラム
シエルである。
第2図に図示の様に本発明の好ましい実施態様
としては予じめ予熱装置内のスクラツプ上に固体
燃料を載置せしめ、次いで高温の排ガスを第2図
中の矢標方向から導入してスクラツプを予熱す
る。もつとも豆炭の如きものを使用する場合はス
クラツプ中に分散させて装入するのが予熱効果を
高める上でよい。又固体燃料を2種以上併用する
場合例えばオガライトと石炭とを併用する場合は
石炭を下にしその上にオガライトを載せるのがよ
い。
本発明の予熱方法に於けるスクラツプの予熱及
び溶解パターン例については第3図に工程フロー
シートを以つて示した。尚第3図中Aが溶解パタ
ーンであり、Bがスクラツプ予熱パターンであ
る。
次に本発明の実施例を示す。
実施例 1
下記組成のスクラツプ31Tonのうち初装分
20Tonを第2図に図示の予熱装置に投入し、当該
スクラツプの上にオガライト105Kgを載置して予
熱を行つた。
スクラツプ組成;
NP〔新断プレスによる鋼板打抜屑〕 18〔Ton〕
特 級 5
クロツプ 7
その他 1
オガライトは着火が早く、急速に燃焼した。
NP材といえども赤熱した。着火後のクラムシエ
ル内の雰囲気温度は約1050℃まで上昇し、燃焼塔
の排ガス温度より高くなつた。尚このクラムシエ
ル内の雰囲気温度及び燃焼塔の排ガス温度並びに
スクラツプ予熱装置(SPH)入力及び出口の温度
測定結果については第4図Bに図示した。又スク
ラツプ温度は平均380℃と高いものであつた。上
記予熱の後同じ組成の追装スクラツプ11Tonを同
予熱装置に装入し固体燃料なしに予熱して溶解炉
に追装した。
そして溶解炉で溶解し、溶製鋼種としてSF系
鋼(炭素鋼)31Tonを得た。この際の電力原単位
(スクラツプ1Tonを溶解するに要する電力、kwt
h/cht)は固体燃料を投入しない場合を100とした
とき95であり、電力消費が極めて少ないことが判
つた。又Tap−Tapに要する時間も低減し得た。
実施例 2
オガライトを45Kg、スクラツプとしてNPを
31Ton〔初装20Ton、追装11Ton〕使用した以外
は実施例1と同様にしてスクラツプを予熱した。
又溶製鋼種としてSF系鋼(炭素鋼)31Tonを得
た。スクラツプ温度は平均360゜であつた。又電
力原単位は固体燃料を投入しない場合を100とし
たとき98であり、電力消費が少ないことを示して
いる。クラムシエル内の雰囲気温度は約950℃と
上昇した。このクラムシエル内の雰囲気温度及び
燃焼塔の排ガス温度並びに予熱装置(SPH)入力
及び出口の温度測定結果については第4図Aに図
示した。
比較例 1
固体燃料を使用しない以外は実施例1と同様に
して予熱を行つたところ、クラムシエル内の雰囲
気温度は600℃程度に留まり、スクラツプ温度は
平均350℃であつた。クラムシエル内の雰囲気温
度及びSPH入力の温度測定結果を第5図に図示し
た。
実施例 3
豆炭を100Kg使用した以外は実施例1と同様に
して予熱を行つた。スクラツプ温度は平均360℃
であつた。電力原単位は固体燃料なし〔比較例
1〕と100としたとき98であつた。
なお豆炭は、発炎性でないため豆炭の周辺のス
クラツプを昇温させるのみで、クラムシエル全体
の雰囲気特に上部の雰囲気温度は上昇しない。ま
た豆炭はスクラツプ中に分散して装入した。
実施例 4
オガライト105Kg、大西炭(中国産)100Kgを使
用した以外は実施例1と同様にして予熱を行つ
た。スクラツプ温度は平均400℃と著しく上昇し
た。又電力原単位は固体燃料なし〔比較例1〕を
100としたとき93と著しく低減した。
以上の実施例1乃至実施例4の試験結果を次の
第2表にまとめて示した。[Table] Shown.
Although the ignition temperature is not shown for the tires in Table 1 above, tires melt and decompose at around 200℃ and become gasified, and the gas is mainly hydrocarbons, so the ignition temperature is around 500℃. It is estimated to be. Therefore, in view of the above-mentioned matters and the data in Table 1 above, the solid fuel of the present invention can be obtained by heating and compressing wood chips such as ogalite and charcoal with or without using a binder. It is preferable to use a solid fuel with a large surface area that has been solidified without any heat loss. Ogalite in particular ignites at a relatively low temperature (200
~300℃), and the temperature after ignition reaches 1000~1100℃ at the top of the clam shell of the preheating device, which is higher than the exhaust gas temperature of the combustion tower. In addition, even if it is difficult to preheat scrap, the preheating effect is enhanced to the point where it becomes red hot, and there is little white smoke. One or more of the above solid fuels may be used. When two or more types are used in combination, the preheating effect can be further enhanced. For example, to explain the combined use of ogalite and coal, ogalite ignites early during preheating, and the flame hits the coal.
Coal, which has a high combustion heat but is difficult to ignite, is ignited and burned. This allows for even more effective use of coal as preheating fuel. In the preheating method of the present invention, scrap is charged into a preheating device, solid fuel is added to the scrap, high temperature exhaust gas discharged from a melting furnace is introduced into the scrap, and the solid fuel is heated using the temperature of the exhaust gas. Preheat the scraps by burning them. According to this method of the present invention, the calorific value of the exhaust gas and the calorific value of the solid fuel combine to raise the gas atmosphere temperature in the preheating device and the scrap temperature more than expected. FIG. 2 shows an embodiment of the preheating method of the present invention and the preheating device used therein. 1 in Figure 2
0 is scrap, 11 is solid fuel, and 12 is clam shell. As shown in FIG. 2, in a preferred embodiment of the present invention, solid fuel is placed on the scrap in the preheating device in advance, and then high-temperature exhaust gas is introduced from the direction of the arrow in FIG. Preheat the scrap. However, when using something like small charcoal, it is better to disperse it in the scrap and charge it in order to enhance the preheating effect. Furthermore, when two or more types of solid fuel are used in combination, for example, when ogalite and coal are used together, it is preferable to place the ogalite on top of the coal with the coal facing down. An example of the scrap preheating and melting pattern in the preheating method of the present invention is shown in a process flow sheet in FIG. In FIG. 3, A is a melting pattern, and B is a scrap preheating pattern. Next, examples of the present invention will be shown. Example 1 First loading of 31 tons of scrap with the following composition
20 tons were put into the preheating device shown in Fig. 2, and 105 kg of Ogalite was placed on top of the scrap to preheat it. Scrap composition: NP [Steel plate punching scrap from new cutting press] 18 [Ton] Special grade 5 Crop 7 Others 1 Ogalite ignited quickly and burned rapidly.
Even though it was NP material, it was red hot. After ignition, the atmospheric temperature inside the clam shell rose to approximately 1050°C, which was higher than the exhaust gas temperature from the combustion tower. The atmospheric temperature in the clam shell, the exhaust gas temperature of the combustion tower, and the temperature measurement results at the input and outlet of the scrap preheater (SPH) are shown in FIG. 4B. In addition, the scrap temperature was as high as 380°C on average. After the above preheating, 11 tons of additional scrap with the same composition was charged into the same preheating device, preheated without solid fuel, and added to the melting furnace. Then, it was melted in a melting furnace to obtain 31 tons of SF steel (carbon steel) as a molten steel type. The power consumption unit (power required to melt 1 ton of scrap, kwt)
h/cht) was 95 when the case without solid fuel input was set to 100, and it was found that the power consumption was extremely low. Also, the time required for Tap-Tap could be reduced. Example 2 45 kg of Ogarite and NP as scrap
Scrap was preheated in the same manner as in Example 1, except that 31 tons (initial loading: 20 tons, additional loading: 11 tons) were used.
In addition, SF steel (carbon steel) of 31 tons was obtained as a steel type. The average scrap temperature was 360°. In addition, the electricity consumption rate is 98 when the case without solid fuel is set as 100, indicating that electricity consumption is low. The atmospheric temperature inside Clamsiel rose to approximately 950℃. The atmospheric temperature in the clam shell, the exhaust gas temperature of the combustion tower, and the temperature measurement results at the input and outlet of the preheater (SPH) are shown in FIG. 4A. Comparative Example 1 When preheating was carried out in the same manner as in Example 1 except that solid fuel was not used, the atmospheric temperature inside the clam shell remained at about 600°C, and the scrap temperature was 350°C on average. The atmospheric temperature inside the clamshell and the temperature measurement results of the SPH input are shown in Figure 5. Example 3 Preheating was carried out in the same manner as in Example 1 except that 100 kg of charcoal was used. Average scrap temperature is 360℃
It was hot. The electricity consumption rate was 98 when compared to the case without solid fuel [Comparative Example 1] as 100. Since the small charcoal is not flammable, it only raises the temperature of the scrap around the small charcoal, and does not raise the temperature of the whole atmosphere of the clam shell, especially the upper part. In addition, the charcoal was dispersed and charged into the scrap. Example 4 Preheating was carried out in the same manner as in Example 1, except that 105 kg of Ogarite and 100 kg of Onishi charcoal (produced in China) were used. The scrap temperature increased significantly to an average of 400℃. Also, the electricity consumption rate is based on the case without solid fuel [Comparative Example 1].
When set to 100, it decreased significantly to 93. The test results of Examples 1 to 4 above are summarized in Table 2 below.
【表】
斯くて、本発明によれば特別の装置を要せずし
て、短時間内に、予熱装置内の排ガスの雰囲気温
度及びスクラツプ自体の温度を著しく上昇せしめ
得、しかも従来法よりもより一層少ない電力消費
で短時間に溶解を可能とするスクラツプの予熱方
法を提供し得た。[Table] Thus, according to the present invention, the ambient temperature of the exhaust gas in the preheating device and the temperature of the scrap itself can be significantly increased within a short time without requiring any special equipment, and moreover, it is possible to significantly increase the temperature of the exhaust gas in the preheating device and the temperature of the scrap itself. It has been possible to provide a method for preheating scrap that enables melting in a short time with even less power consumption.
図面は本発明の実施例を示し、第1図は本発明
予熱方法に於けるスクラツプ予熱装置系統図、第
2図は本発明の方法及びそれに使用する装置を説
明する為の要部断面図、第3図は本発明方法に於
ける予熱、溶解パターンの工程フロー図、第4図
は本発明の効果を示すグラフ、第5図は従来法に
よる排ガス雰囲気温度を示すグラフである。
1……溶解炉、2……電極、3……ダクト、1
0……スクラツプ、11……固体燃料。
The drawings show embodiments of the present invention; FIG. 1 is a system diagram of a scrap preheating device in the preheating method of the present invention; FIG. 2 is a sectional view of essential parts for explaining the method of the present invention and the apparatus used therein; FIG. 3 is a process flow diagram of preheating and melting patterns in the method of the present invention, FIG. 4 is a graph showing the effects of the present invention, and FIG. 5 is a graph showing the exhaust gas atmosphere temperature according to the conventional method. 1... Melting furnace, 2... Electrode, 3... Duct, 1
0...Scrap, 11...Solid fuel.
Claims (1)
て製鋼用スクラツプを予熱する製鋼用スクラツプ
の予熱方法に於いて、製鋼用スクラツプに固体燃
料を添加し、該固体燃料を排ガスにより燃焼させ
て予熱を行うことを特徴とする製鋼用スクラツプ
の予熱方法。1 In a method for preheating steelmaking scrap that uses high-temperature exhaust gas discharged from a melting furnace, solid fuel is added to steelmaking scrap, and the solid fuel is combusted by the exhaust gas to preheat it. A method for preheating steelmaking scrap, characterized by performing the following steps.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17238081A JPS5872878A (en) | 1981-10-28 | 1981-10-28 | Method of preheating scrap |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17238081A JPS5872878A (en) | 1981-10-28 | 1981-10-28 | Method of preheating scrap |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5872878A JPS5872878A (en) | 1983-04-30 |
| JPS6146751B2 true JPS6146751B2 (en) | 1986-10-15 |
Family
ID=15940832
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17238081A Granted JPS5872878A (en) | 1981-10-28 | 1981-10-28 | Method of preheating scrap |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5872878A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6233711A (en) * | 1985-08-06 | 1987-02-13 | Yamaguchi Kyoei Kogyo Kk | Method for preheating scrap |
-
1981
- 1981-10-28 JP JP17238081A patent/JPS5872878A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5872878A (en) | 1983-04-30 |
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