JPS63121607A - Method for operating blast furnace - Google Patents

Method for operating blast furnace

Info

Publication number
JPS63121607A
JPS63121607A JP26642186A JP26642186A JPS63121607A JP S63121607 A JPS63121607 A JP S63121607A JP 26642186 A JP26642186 A JP 26642186A JP 26642186 A JP26642186 A JP 26642186A JP S63121607 A JPS63121607 A JP S63121607A
Authority
JP
Japan
Prior art keywords
blast furnace
petroleum coke
blow pipe
pulverized coal
lance
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.)
Pending
Application number
JP26642186A
Other languages
Japanese (ja)
Inventor
Yoshimi Kamitsuma
上妻 義美
Masayuki Fukui
雅之 福井
Toshinari Kumada
熊田 登志也
Yoshitoshi Tanimura
谷村 俊寿
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.)
NAKAYAMA SEIKOSHO KK
Nakayama Steel Works Ltd
Original Assignee
NAKAYAMA SEIKOSHO KK
Nakayama Steel Works Ltd
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 NAKAYAMA SEIKOSHO KK, Nakayama Steel Works Ltd filed Critical NAKAYAMA SEIKOSHO KK
Priority to JP26642186A priority Critical patent/JPS63121607A/en
Publication of JPS63121607A publication Critical patent/JPS63121607A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/001Injecting additional fuel or reducing agents
    • C21B5/003Injection of pulverulent coal

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To efficiently use petroleum coke by blowing a mixture composed of petroleum coke and fine coal mixed at a prescribed ratio into a blow pipe for blowing hot wind through a lance on an upper stream side at the contact point between the lance and the blow pipe. CONSTITUTION:The petroleum coke 6 is mixed with the fine coal 5 before the contact point between the blow pipe 2 for blowing hot wind connected to a tuyere 1 of a blast furnace and the lance 3 for blowing solid fuel. The mixture is blown from the lance 3 into the blow pipe 2 at the mixing ratio thereof petroleum coke/fine coal) specified to >=20%. The existing blow pipe 2 is thus smoothly utilized and the efficient combustion efficiency is obtd.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は高炉の操業方法に関するものである。[Detailed description of the invention] Industrial applications The present invention relates to a method of operating a blast furnace.

従来の技術 従来、高炉の操業において、羽目への吹き込み燃料は、
石油価格の高騰の影響を受けて、液体(オイル)の単独
吹き込みから、固体(微粉炭)吹き込み技術の導入が図
られ、現在、微粉炭吹き込みが主流となっている。
Conventional technology In the past, in blast furnace operation, the fuel blown into the siding was
In response to the soaring oil prices, attempts were made to introduce solid (pulverized coal) injection technology instead of liquid (oil) injection, and pulverized coal injection has now become the mainstream.

発明が解決しようとする問題点 しかしながら、固体(微粉炭)吹き込みは、液体(オイ
ル)吹き込みに比較して、燃焼速度が遅く、かつ、灰分
という未燃分を含有し、発熱量も低いため、微粉炭の高
炉吹き込みの実用化にあたっては、石炭の銘柄選定に苦
慮するとともに、炉内コークスとの置換率において、液
体燃料(オイル)より、劣っていることが、大きな問題
であった。
Problems to be Solved by the Invention However, compared to liquid (oil) injection, solid (pulverized coal) injection has a slower combustion rate, contains unburned ash, and has a lower calorific value. When putting pulverized coal into blast furnace injection into practical use, it was difficult to select a brand of coal, and a major problem was that it was inferior to liquid fuel (oil) in terms of replacement rate with coke in the furnace.

第1表 第1表は、その問題点について、固体燃料(微粉炭)、
液体燃料(オイル)を例にとり示したものである。
Table 1 Table 1 shows the problems of solid fuel (pulverized coal), solid fuel (pulverized coal),
This is an example of liquid fuel (oil).

固体燃料(微粉炭)は粉砕性より、HGIの制限(一般
に40以上)また燃焼性の面、高炉操業安定性の面から
Ashの制限等、規制が多く液体燃料(オイル)に比較
して、使用上、煩雑な燃料であることがわかる。更に、
固体燃料(微粉炭)の発熱量は、液体燃料(オイル)よ
り木質的に低い、その結果、高炉での実質的使用効果を
示す、コークスとの置換率は、液体燃料(オイル)の7
〜8割どまりであり、この劣性要因を改善することは、
不可能とされていた。
Compared to liquid fuel (oil), solid fuel (pulverized coal) has many regulations such as restrictions on HGI (generally 40 or more) and Ash restrictions on combustibility and stability of blast furnace operation. It can be seen that it is a complicated fuel to use. Furthermore,
The calorific value of solid fuel (pulverized coal) is woody lower than that of liquid fuel (oil).As a result, it shows a substantial use effect in blast furnaces, and the replacement rate with coke is 7
~80%, and improving this recessive factor is
It was considered impossible.

そこで、本発明は、微粉炭を高炉羽目迄、圧送する公知
の微粉炭設備において、被圧送物である従来の微粉化さ
れた石炭系固体燃料に対し、石油系の固体燃料の一種で
ある石油コークスを、20%以上の範囲で混合、もしく
は、全量、高炉羽口へ供給することにより、石炭系固体
燃料では、木質的に達成不可能であったオイルなみの高
カロリー、低Ashを享受し高炉の操業改善を図ろうと
するものである。
Therefore, in a known pulverized coal facility that pumps pulverized coal to the blast furnace, the present invention aims to replace the conventional pulverized coal-based solid fuel, which is the material to be pumped, with petroleum oil, which is a type of petroleum-based solid fuel. By mixing coke in a range of 20% or more or supplying the entire amount to the blast furnace tuyere, it is possible to enjoy the high calorie and low Ash of oil, which was impossible to achieve with coal-based solid fuel due to its wood quality. The aim is to improve the operation of blast furnaces.

問題点を解決するための手段 本発明は第1図に示すように高炉羽口(1)に連接され
た熱風吹き込み用ブローパイプ(2)内へ、固体燃料(
微粉炭用石炭)(5)を供給し、かつ。
Means for Solving the Problems The present invention, as shown in FIG. 1, injects solid fuel (
pulverized coal) (5), and.

燃焼を生じせしめる固体燃料吹き込みランス(3)とブ
ローパイプ(2)の接点(4)以nηで石油コークス(
8)を、微粉炭用石炭(5)中に混合し、その混合比率
を20%以上吹き込むことにより、高炉羽目(1)への
既公知微粉炭吹き込み設備を円滑に活用し高炉にとって
より効果的な燃焼効率を得ることを特徴とするものであ
る。
Petroleum coke (
By mixing 8) into the coal for pulverized coal (5) and injecting it at a mixing ratio of 20% or more, the known pulverized coal injection equipment into the blast furnace siding (1) can be smoothly utilized, making it more effective for the blast furnace. It is characterized by obtaining high combustion efficiency.

作用 木発りIの高炉操業法によれば、固体燃′!4(微粉炭
田石炭)中に混合する石油コークス混合率が0〜20%
では、石油コークス混合効果は殆ど現われていないが、
高炉での操業効果を見る場合、−般に燃料比が用いられ
ており、石油コークス混合率が20%以上になると、高
炉の燃料比低下は顕著であり、コークスとの置換率で1
.0以上が得られ、微粉炭吹き込み時のコークスとの置
換率0.93から大幅に上昇した。
According to the operating method of the blast furnace I, solid combustion '! 4 (Pulverized coalfield coal) has a petroleum coke mixing ratio of 0 to 20%.
In this case, the petroleum coke mixing effect hardly appears,
When looking at the operational effects of blast furnaces, the fuel ratio is generally used, and when the petroleum coke mixing ratio exceeds 20%, the fuel ratio in the blast furnace decreases significantly, and the replacement ratio with coke increases by 1.
.. 0 or more was obtained, which significantly increased from the coke replacement ratio of 0.93 during pulverized coal injection.

実施例 本発明では液体燃料(オイル)に比較して劣る微粉石炭
系固体燃料に対し、石油系の固体燃料の一種である石油
コークスを混合使用するもので、固定燃料の範略におい
て、液体燃料(オイル)の発熱量、Ash、燃焼性に最
も類似するものを調査、検討した。
Example In the present invention, petroleum coke, which is a type of petroleum-based solid fuel, is used in combination with pulverized coal-based solid fuel, which is inferior to liquid fuel (oil). We investigated and examined the most similar calorific value, Ash, and combustibility of (oil).

下記の第2表は、その調査、およびテスト結果を示す。Table 2 below shows the research and test results.

第2表 この表から発熱量、Ashとも、石油コークスが最も優
れていることが分かる。ただし着火温度が高いこと、又
揮発分が低いことは、燃焼性に悪影響を及ぼすことも考
えられるため、実炉において燃焼状況良否判定テストを
実施した。
Table 2 From this table, it can be seen that petroleum coke is the best in both calorific value and Ash. However, a high ignition temperature and low volatile content may have a negative effect on combustibility, so a test was conducted to determine the quality of combustion in an actual furnace.

第3表に、そのテスト時に供した固体燃料の性状を示す
Table 3 shows the properties of the solid fuel used during the test.

第3表 また第1図に燃焼テスト時の吹き込み部の[嬰を示すも
ので、(1)は高炉羽口、(2)はブローパイプ、(3
)は固体燃料吹き込みランス、(4)はブローパイプと
固体燃料吹き込みランスとの接点、(5)は微粉炭、(
6)は石油コークス、(7)は覗き窓を示し、第2図(
A)(B)に1羽口部の燃焼状況良否判定項目の1つで
ある羽口へのAsh付着目視観察例を示し、(8)は羽
口部に付着したAshである。
Table 3 and Figure 1 show the blowing part during the combustion test, (1) is the blast furnace tuyere, (2) is the blow pipe, (3) is the blast furnace tuyere, (2) is the blow pipe,
) is the solid fuel injection lance, (4) is the contact point between the blow pipe and the solid fuel injection lance, (5) is the pulverized coal, (
6) shows the petroleum coke, (7) shows the viewing window, and Figure 2 (
A) and (B) show examples of visual observation of Ash adhesion to the tuyere, which is one of the criteria for determining the quality of the combustion status of one tuyere, and (8) shows Ash adhering to the tuyere.

燃焼テスト実施時のテスト条件は、下記の通りである。The test conditions when conducting the combustion test are as follows.

炉  内  容  積          1000m
”風        Hk、           1
f30ON m’ / rIi n熱  風  温  
度          1200℃熱  風  圧  
力         2.5  Kg/ Cm″固体燃
料吹き込み速度   400Kg / Hr・羽口(微
粉炭用石炭十石油コークス) 羽口先理論燃焼ガス温度  2300℃羽 口 木 数
      10本(全羽口20本)テスト方法は、石
油コークス混合率(=石油コークス吹き込み量/微粉炭
用石炭吹き込み量)を0%から100%まで増大させ、
羽口へのAsh付着を生じさせないこと、又高炉ガス清
浄設Ja(シックナー)にススの発生を生じさせないこ
とを条件に、羽目部で燃焼に必要な酸素使用量をもとめ
た。
Furnace inner volume 1000m
``Wind Hk, 1
f30ON m' / rIi n heat wind temperature
degree 1200℃ heat wind pressure
Force 2.5 Kg/Cm'' Solid fuel injection speed 400Kg/Hr・Tuyere (coal and petroleum coke for pulverized coal) Theoretical combustion gas temperature at tuyere tip 2300℃ Tuyere Number of trees 10 (20 tuyeres in total) Test method increases the petroleum coke mixing ratio (= petroleum coke injection amount/pulverized coal injection amount) from 0% to 100%,
The amount of oxygen required for combustion at the tuyeres was determined on the condition that ash would not adhere to the tuyeres and soot would not be generated in the blast furnace gas cleaning equipment Ja (thickener).

第3図に、そのテスト結果を示す8羽口部のAsh付着
のない条件で、石油コークス混合率を上昇すると、#素
使用量を増大させる必要はなく。
FIG. 3 shows the test results.If the petroleum coke mixing ratio is increased under the condition that there is no ash adhesion at the tuyeres, there is no need to increase the amount of # element used.

むしろ減少していることから高炉羽口部での燃焼状況の
改善に有効との知見を得た。
In fact, it was found to be effective in improving the combustion conditions at the blast furnace tuyere.

したがって、石油コークスが、発熱量、Ash、燃焼性
等、高炉に最も適した固体燃料であることを確認するた
めには、高炉での総合効果の把握が必要である。
Therefore, in order to confirm that petroleum coke is the most suitable solid fuel for blast furnaces in terms of calorific value, Ash, combustibility, etc., it is necessary to understand the overall effects in blast furnaces.

そこで、現状の微粉炭操業と本発明の石油コークス混合
吹き込みの効果を確認するため、高炉操業実炉テストを
行った。
Therefore, in order to confirm the effects of the current pulverized coal operation and the mixed injection of petroleum coke of the present invention, an actual blast furnace operation test was conducted.

以下に、その実施内容、および、テスト結果を示す。The implementation details and test results are shown below.

高炉操業実炉テスト実施時のテスト条件は、下記の通り
である。
The test conditions during actual blast furnace operation test are as follows.

炉  内  容  積          1000m
’風     量      188ON m’ / 
mi n熱  風  温  度          1
200℃熱  風  圧  力         2.
5  Kg/ Cm’酸素使用m         8
00 N m” / Hr固体燃料吹き込み速度   
400Kg / Hr °羽口(微粉炭用石炭十石油コ
ークス) 羽口先理論燃焼ガス温度  2300℃羽  口  木
  数         全羽目20本また、そのテス
ト結果を、第4図、第5図に示す。
Furnace inner volume 1000m
'Air volume 188ON m' /
min heat wind temperature 1
200℃ heat air pressure 2.
5 Kg/ Cm'Oxygen usage m 8
00 N m”/Hr solid fuel injection speed
400Kg/Hr °Tuyere (coal for pulverized coal, petroleum coke) Theoretical combustion gas temperature at the tip of the tuyere: 2300°C Number of tuyeres: 20 in total The test results are shown in Figures 4 and 5.

第4図は1石油コークス混合率の増大によって、炉内で
完全にガス化せず、未燃カーボンが高炉ダストとして炉
外排出していないかどうかを確認調査したものである。
Figure 4 shows an investigation to confirm whether or not unburned carbon was discharged outside the furnace as blast furnace dust due to the increase in the petroleum coke mixing ratio, resulting in complete gasification in the furnace.

全ての混合率にわたって高炉乾式ダスト発生比は、略1
5Kg/l−Pで、一定しており、石油コークス混合率
上昇による悪影響は、皆無であった。
Over all mixing ratios, the blast furnace dry dust generation ratio is approximately 1
It was constant at 5Kg/l-P, and there was no adverse effect due to the increase in the petroleum coke mixing ratio.

高炉での操業効果を見る場合、一般に燃焼比が用いられ
る。従って、第5図は、未発01Jの効果を、石油コー
クス混合率と高炉燃料比の関係で示したものである。
Combustion ratio is generally used when looking at the operational effects of blast furnaces. Therefore, FIG. 5 shows the effect of unexploded 01J in terms of the relationship between the petroleum coke mixing ratio and the blast furnace fuel ratio.

石油コークス混合率が0〜20%では、石油コークス混
合効果は、殆ど現れていない。
When the petroleum coke mixing ratio is 0 to 20%, the petroleum coke mixing effect hardly appears.

石油コークス混合率が20%以上になると、高炉の燃料
比低下は、顕著であり、コークスとの置換率で、1.0
以上が得られ、微粉炭吹き込み時のコークスとの置換率
0.93から、大幅に上昇した。
When the petroleum coke mixing ratio exceeds 20%, the fuel ratio in the blast furnace decreases significantly, and the replacement ratio with coke is 1.0%.
The above results were obtained, and the replacement rate with coke at the time of pulverized coal injection was significantly increased from 0.93.

したがって、本発明では1石油コークスを最も効果的に
使用できる混合率が20%以上であることから、この範
囲に限定して使用することとしたものである。
Therefore, in the present invention, since the mixing ratio at which petroleum coke can be used most effectively is 20% or more, the use is limited to this range.

発明の効果 以上の説明より、従来の微粉炭操業法が同種の固体燃料
(石炭系の固体燃料であれば複数銘柄でも同種とする。
Effects of the Invention From the above explanation, it is clear that the conventional pulverized coal operation method uses the same type of solid fuel (if it is a coal-based solid fuel, the same type is used even if multiple brands are used).

)のみ使用していたのに対し、本発明では、異種の固体
燃料、即ち、石油系の石油コークスで最も効果的な使用
法を提供しうるちのであり、高炉操業上、極めて有効な
操業方法である。
), whereas the present invention provides the most effective method of using a different type of solid fuel, that is, petroleum-based petroleum coke, and is an extremely effective operating method for blast furnace operation. It is.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明方法による固体燃料吹き込み部の拡大
図、第2図(λ)(B)は、ブーロバイブに取りつけら
れた覗き窓から羽目部を目視した概要図で、(A)はA
sh付着なし、(B)はAsh付着ありの状態を示す、
第3図は、石油コークス混合率と酸素使用量の関係を示
すグラフ、第4図は、石油コークス混合率と乾式ダスト
発生比の関係を示すグラフ、第5図は石油コークス混合
率と高炉燃料比の関係を示すグラフ。 (1)・・・羽口、(2)・・・ブローパイプ。 (3)・・−固体燃料吹き込みランス、(4)・・・ブ
ローパイプと固体燃料吹き込みランスの接点、(5)・
―・微粉炭、(6)・・・石油コークス、(7)・Φ・
覗き窓、(8)−・・羽口部に付着したAsh。 特許出願人 株式会社 中 山 製 鋼 所第 1 図 第 2 図 (A)         (B) Φ 第 3 図 匁報(I1巽く ≧
FIG. 1 is an enlarged view of the solid fuel injection section according to the method of the present invention, FIG.
No sh adhesion, (B) shows the state with Ash adhesion,
Figure 3 is a graph showing the relationship between petroleum coke mixing ratio and oxygen consumption, Figure 4 is a graph showing the relationship between petroleum coke mixing ratio and dry dust generation ratio, and Figure 5 is a graph showing petroleum coke mixing ratio and blast furnace fuel. A graph showing the relationship between ratios. (1)...Tuyere, (2)...Blowpipe. (3)...-Solid fuel injection lance, (4)...Contact point between blow pipe and solid fuel injection lance, (5)...
―・Pulverized coal, (6)・・・Petroleum coke, (7)・Φ・
Peephole, (8) - Ash attached to the tuyere. Patent applicant: Nakayama Steel Co., Ltd. Figure 1 Figure 2 (A) (B) Φ Figure 3

Claims (1)

【特許請求の範囲】[Claims] 1、高炉羽口に連接された熱風吹き込み用ブローパイプ
内へ、固体燃料を供給し、かつ、燃焼を生じせしめるラ
ンスとブローパイプの接点以前で石油コークスを、微粉
炭用石炭中に混合し、その混合比率を20%以上吹き込
むことにより、高炉羽口への既公知微粉炭吹き込み設備
を円滑に活用し高炉にとってより効果的な燃焼効率を得
ることを特徴とする高炉の操業方法。
1. Supplying solid fuel into the blow pipe for blowing hot air connected to the blast furnace tuyeres, and mixing petroleum coke with coal for pulverized coal before the contact point between the lance and the blow pipe that causes combustion, A method for operating a blast furnace, characterized in that by injecting pulverized coal at a mixing ratio of 20% or more, known pulverized coal injection equipment into the blast furnace tuyere can be smoothly utilized to obtain more effective combustion efficiency for the blast furnace.
JP26642186A 1986-11-08 1986-11-08 Method for operating blast furnace Pending JPS63121607A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26642186A JPS63121607A (en) 1986-11-08 1986-11-08 Method for operating blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26642186A JPS63121607A (en) 1986-11-08 1986-11-08 Method for operating blast furnace

Publications (1)

Publication Number Publication Date
JPS63121607A true JPS63121607A (en) 1988-05-25

Family

ID=17430698

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26642186A Pending JPS63121607A (en) 1986-11-08 1986-11-08 Method for operating blast furnace

Country Status (1)

Country Link
JP (1) JPS63121607A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104060006A (en) * 2013-04-18 2014-09-24 攀钢集团攀枝花钢铁研究院有限公司 Material for injection, application and method thereof for blast furnace smelting
JP2015166485A (en) * 2014-03-04 2015-09-24 株式会社神戸製鋼所 Method for operating petroleum coke injection blast furnace
JP2018168416A (en) * 2017-03-29 2018-11-01 新日鐵住金株式会社 Blast furnace operation method
JP2019019347A (en) * 2017-07-12 2019-02-07 新日鐵住金株式会社 Method of operating blast furnace

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60131905A (en) * 1983-12-21 1985-07-13 Nisshin Steel Co Ltd Method for supplying fuel to blast furnace tuyere

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Publication number Priority date Publication date Assignee Title
JPS60131905A (en) * 1983-12-21 1985-07-13 Nisshin Steel Co Ltd Method for supplying fuel to blast furnace tuyere

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104060006A (en) * 2013-04-18 2014-09-24 攀钢集团攀枝花钢铁研究院有限公司 Material for injection, application and method thereof for blast furnace smelting
CN104060006B (en) * 2013-04-18 2016-04-06 攀钢集团攀枝花钢铁研究院有限公司 The method of winding-up material and application and blast-furnace smelting
JP2015166485A (en) * 2014-03-04 2015-09-24 株式会社神戸製鋼所 Method for operating petroleum coke injection blast furnace
JP2018168416A (en) * 2017-03-29 2018-11-01 新日鐵住金株式会社 Blast furnace operation method
JP2019019347A (en) * 2017-07-12 2019-02-07 新日鐵住金株式会社 Method of operating blast furnace

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