WO2015146872A1 - 酸素高炉の操業方法 - Google Patents
酸素高炉の操業方法 Download PDFInfo
- Publication number
- WO2015146872A1 WO2015146872A1 PCT/JP2015/058656 JP2015058656W WO2015146872A1 WO 2015146872 A1 WO2015146872 A1 WO 2015146872A1 JP 2015058656 W JP2015058656 W JP 2015058656W WO 2015146872 A1 WO2015146872 A1 WO 2015146872A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- tuyere
- gas
- blast furnace
- blowing
- oxygen
- Prior art date
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/06—Making pig-iron in the blast furnace using top gas in the blast furnace process
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B5/003—Injection of pulverulent coal
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B2005/005—Selection or treatment of the reducing gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
- F27D2019/0028—Regulation
- F27D2019/0075—Regulation of the charge quantity
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Definitions
- the present invention relates to a method of operating an oxygen blast furnace in which pure oxygen is supplied from the tuyere and blast furnace gas with less nitrogen is generated from the top of the furnace.
- a general blast furnace blows hot air from the tuyere, and a mixed gas (M gas) made by mixing gases generated from a blast furnace, coke oven, converter, etc. is used as the heat source for obtaining the hot air. Is done.
- M gas mixed gas
- the reducing material ratio in the blast furnace is reduced by the amount of heat of the hot air. Since reducing materials used in conventional blast furnaces are mainly made of fossil fuel mainly composed of carbon, it can be said that hot air blowing suppresses the amount of fossil fuel used and the amount of CO 2 generated. .
- an oxygen blast furnace for producing hot metal by blowing pure oxygen at room temperature from the tuyere instead of the hot stove has been proposed (see Patent Document 1).
- the purpose of this oxygen blast furnace was to generate and recover a blast furnace gas substantially free of nitrogen and use it as a gas for the synthetic chemical industry.
- this oxygen blast furnace since pure oxygen was blown from the tuyere and reacted with coke, there was a technical problem that the temperature at the tuyere tip was abnormally high.
- Patent Document 1 describes a method of controlling the temperature within a predetermined temperature range by blowing CO 2 -containing furnace top gas from the tuyere. Patent Document 1 also proposes a method of blowing H 2 O or CO 2 from the tuyere. Furthermore, as another method, a technique of blowing heavy oil from the tuyere has been proposed (see Patent Document 2).
- Patent Document 3 proposes a coal dry distillation gasification method in which C gas generated from a coke oven is blown into a tuyere to be desulfurized and reformed.
- these are technologies unrelated to the tuyere tip temperature control.
- the oxygen blast furnace of the type in which pure oxygen is blown from the tuyere instead of hot air has a characteristic that the tuyere tip temperature becomes extremely high, and the tuyere tip temperature is lowered well. It is essential to operate.
- the tuyere tip does not become abnormally hot, which is a technical problem peculiar to an oxygen blast furnace.
- H 2 O or CO 2 is blown together with normal temperature pure oxygen from the tuyere and the following endothermic reaction is induced to lower the tuyere tip temperature.
- the reaction at this time is an endothermic reaction of combustion (oxidation) and reverse reaction (reduction), and the temperature of the tuyere at an abnormally high temperature can be lowered.
- the reactions of the following formulas (1) and (2) consume solid carbon at the tuyere (raceway), the amount of coke used increases.
- the oxygen blast furnace there is a problem that an increase in the amount of fossil fuel used and an increase in the amount of generated CO 2 occur.
- the object of the present invention is to propose an operating method of an oxygen blast furnace capable of solving the above-mentioned problems of the prior art and lowering the temperature in the combustion region of the tuyere by reducing CO 2 emissions compared to the conventional technique. There is to do.
- Another object of the present invention is to propose a method for operating an oxygen blast furnace capable of avoiding the occurrence of soot that becomes a problem with the use of heavy oil and realizing stable injection of pure oxygen from the tuyere.
- the present invention which was developed to achieve the above object, is a method of operating an oxygen blast furnace in which at least pure oxygen is blown from the tuyere and blast furnace gas with less nitrogen is generated from the top of the furnace, together with the blowing of pure oxygen from the tuyere.
- a method of operating an oxygen blast furnace characterized by lowering the temperature in the combustion region at the tip of the tuyere by blowing from the tuyere the tuyere injecting gas in which the sum of the volume fractions of hydrocarbon and hydrogen is 50% or more It is.
- the operation method of the oxygen blast furnace of the present invention pure oxygen is blown from the tuyere, and tuyere blown gas in which the sum of the volume fractions of hydrocarbon and hydrogen is 50% or more is blown from the tuyere.
- the abnormal high temperature in the tuyere tip combustion region which is a problem specific to the oxygen blast furnace, can be prevented and the temperature can be lowered.
- the present invention has an effect of reducing CO 2 emission compared with the tuyere tip temperature reduction method used in the conventional oxygen blast furnace operating method.
- FIG. 1 is a diagram showing an example of an oxygen blast furnace and peripheral equipment that are targets of an operation method according to the present invention.
- 1 is an oxygen blast furnace
- 2 is a mixer for mixing gas
- 3 is a burner that preheats the gas to obtain preheated gas (SGI)
- 4 is a generator that generates electricity using blast furnace exhaust gas
- 5 is an oxygen plant for producing pure oxygen
- 6 is a tuyere used for injecting oxygen into the oxygen blast furnace 1.
- ore and coke are introduced from the top in the oxygen blast furnace 1 as in the conventional blast furnace.
- pure oxygen at room temperature is blown from the lower tuyere 6.
- Pure oxygen is produced from the air using a separation technique such as cryogenic separation in the oxygen plant 5 and consumes electric power. Therefore, a method is used in which a coke oven gas, a blast furnace gas, or a mixture of these, which is a combustion gas containing a large amount of CO, is used to generate power with the power generator 4 and produce pure oxygen with the power.
- tuyeres blowing gas such as pulverized coal, natural gas and coke oven gas is also blown from the lower tuyere 6.
- the tuyere 6 uses a tuyere containing an oxygen-pulverized coal burner such as the tuyere described in JP-A-63-171811, and the pulverized coal and tuyere blowing gas from the internal burner, Pure oxygen can be blown from the outside tuyere.
- an oxygen-pulverized coal burner such as the tuyere described in JP-A-63-171811
- Pure oxygen can be blown from the outside tuyere.
- one burner is arranged in the tuyere and either pulverized coal and tuyere blowing gas are mixed and blown from the burner, or two burners are arranged in the tuyere, one from the pulverized coal, and the other from the tuyere It is advisable to blow in gas.
- the oxygen blast furnace 1 has a problem that the temperature at the top of the furnace is lowered because the gas flow rate is small.
- the temperature of the furnace top gas becomes 100 ° C. or lower, condensation occurs at the top of the furnace, causing operational troubles. Therefore, in order to keep the temperature at the top of the furnace at 100 ° C. or higher, as shown in FIG. 1, a part of the blast furnace exhaust gas (B gas) that is a combustion gas containing a large amount of CO is circulated and flows into the burner 3. It is good to use the method of making it burn and making high temperature preheating gas (SGI), and blowing from a blast furnace shaft part.
- SGI high temperature preheating gas
- the tuyere tip temperature is preferably about 2000 ° C. to 2600 ° C. If the tuyere temperature is less than 2000 ° C., as described in Japanese Patent Application Laid-Open No. 2003-247008, combustion of pulverized coal becomes insufficient, resulting in an increase in unburned char, There is a concern that the pressure loss will increase. On the other hand, in an oxygen blast furnace, pure oxygen at room temperature is blown from the tuyere at a high flow rate (100 m / s or more) instead of hot air (1000 ° C. or more), so that the tuyere cooling effect by oxygen at room temperature can be obtained.
- the tuyere tip temperature is lowered when a gas blowing material containing hydrocarbon or hydrogen is blown, it is preferable to adjust the blowing amount of the gas blowing material in order to set the tuyere tip temperature to an appropriate temperature.
- Even pulverized coal can be expected to have a tuyere tip temperature reduction effect similar to that of a gas blowing material containing hydrocarbons or hydrogen, but if it is blown too much, pressure loss in the furnace increases and operation becomes unstable. Therefore, the tuyere temperature cannot be lowered to an appropriate temperature only with pulverized coal. Therefore, for controlling the tuyere temperature (lowering the temperature), it is preferable to use a gas blowing material containing hydrocarbon or hydrogen.
- the tuyere temperature can be reduced even by blowing heavy oil, as mentioned above, since there is a risk of wrinkles, it is not possible to blow a large amount. In this sense, it is difficult to sufficiently reduce the tuyere temperature of the oxygen blast furnace by blowing heavy oil.
- the total content of hydrogen and hydrocarbon in the tuyere blowing gas needs to be 50% or more in terms of volume fraction. The reason is that if the total ratio of hydrogen and hydrocarbons in the tuyere blowing gas is less than 50%, the tuyere cooling capacity is lowered, and the tuyere tip temperature cannot be lowered sufficiently. If the content of hydrogen and hydrocarbons is less than 50% and the tip temperature is to be lowered to an appropriate temperature, an oxide-based tuyere coolant such as CO 2 or H 2 O together with hydrogen or hydrocarbons Need to blow. Since it would consume the coke solution loss reaction, CO 2 generation amount increases as a result.
- an oxide-based tuyere coolant such as CO 2 or H 2 O together with hydrogen or hydrocarbons Need to blow. Since it would consume the coke solution loss reaction, CO 2 generation amount increases as a result.
- an oxygen blast furnace having an output ratio of 5, a furnace internal volume of 2515 mm 3 and an output amount of 12573 t / day is assumed, and the configuration of the oxygen blast furnace and peripheral equipment is the configuration shown in FIG.
- the tuyere used the form as shown in FIG. 2 in which the burner tube 7 was built in the tuyere. Then, pulverized coal and tuyere blowing gas were blown through the burner tube 7, and pure oxygen at 25 ° C. was blown from between the tuyere and the burner tube 7.
- the burner tube 7 had an outer diameter of 89 mm, and the tuyere had an inner diameter of 140 mm.
- Example suitable for the present invention, conditions for injecting natural gas, coke oven gas (C gas), and propane gas as the tuyere blowing gas were considered. Moreover, as a comparative example, it was set as the method of blowing in blast furnace gas, heavy oil, and water vapor
- Table 1 shows examples of the conditions under which the tuyere temperature was controlled to 2600 ° C. or less, the blowing amount of the tuyere blowing material, the ratio of hydrogen to hydrocarbon in the tuyere blowing gas, and the tuyere tip temperature in the comparative example.
- FIG. 3 shows the evaluation results of the CO 2 emission amount. It can be seen from FIG. 3 that the conventional method of blowing blast furnace gas and steam blows CO 2 emissions larger than that of the conventional blast furnace. This is because the blowing material itself is an oxide such as CO 2 and H 2 O, and coke is consumed when these are once thermally decomposed into CO and H 2 . In addition, the conventional method of heavy oil injection and pulverized coal injection resulted in less CO 2 emissions than the conventional blast furnace, but these were difficult to implement because of the restrictions on the generation of soot and the upper limit of the pulverized coal combustion rate. It was.
- FIG. 4 shows the relationship between the sum of the volume fractions of hydrogen and hydrocarbons in the tuyere blowing gas and CO 2 emissions.
- the biogas conditions are also shown. It can be seen that as the ratio of the coke oven gas increases, the sum of the volume fractions of hydrogen and hydrocarbons increases and the CO 2 emission decreases. When this is compared with the CO 2 emission amount of the conventional blast furnace, if the ratio of hydrogen and hydrocarbons in the tuyere blowing gas is 50% or more, the CO 2 emission amount is smaller than that of the conventional blast furnace. From the above, it was confirmed that the ratio of hydrogen to hydrocarbon should be 50% or less.
- the operation method of the oxygen blast furnace according to the present invention described above can lower the temperature of the tuyere tip combustion region by reducing CO 2 emission compared to the conventional one, and avoid the occurrence of soot that becomes a problem when using heavy oil. Furthermore, since stable pure oxygen can be blown from the tuyere, it can be suitably applied to the operation of the oxygen blast furnace.
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
Description
H2O+C→H2+CO (1)
CO2+C→2CO (2)
また、本発明の他の目的は、重油の使用で問題となる煤の発生を回避し、羽口から純酸素の安定した吹き込みを実現できる酸素高炉の操業方法を提案することにある。
(1)前記羽口吹き込みガスとして、天然ガス、プロパンガス、コークス炉ガス(Cガス)またはバイオガスを用いること、
(2)前記羽口吹き込みガスとして、高炉ガスとコークス炉ガスとの混合ガスを用いること、
がより好ましい解決手段となるものと考えられる。
2 混合機
3 バーナー
4 発電機
5 酸素プラント
6 羽口
7 バーナー管
Claims (3)
- 羽口から少なくとも純酸素を吹き込み、炉頂から窒素の少ない高炉ガスを発生せしめる酸素高炉の操業方法において、前記羽口からの純酸素の吹き込みとともに、その羽口から炭化水素と水素の体積分率の和が50%以上となる羽口吹き込みガスを吹き込むことにより、羽口先の燃焼領域の温度を低下させることを特徴とする酸素高炉の操業方法。
- 前記羽口吹き込みガスとして、天然ガス、プロパンガスコークス炉ガス(Cガス)またはバイオガスを用いることを特徴とする請求項1に記載の酸素高炉の操業方法。
- 前記羽口吹き込みガスとして、高炉ガスとコークス炉ガスとの混合ガスを用いることを特徴とする請求項1に記載の酸素高炉の操業方法。
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016510317A JP6229863B2 (ja) | 2014-03-26 | 2015-03-23 | 酸素高炉の操業方法 |
EP15768555.3A EP3124626B1 (en) | 2014-03-26 | 2015-03-23 | Method of operating oxygen blast furnace |
CN201580015653.XA CN106103746B (zh) | 2014-03-26 | 2015-03-23 | 氧气高炉的操作方法 |
KR1020167025284A KR20160120334A (ko) | 2014-03-26 | 2015-03-23 | 산소 고로의 조업 방법 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2014063802 | 2014-03-26 | ||
JP2014-063802 | 2014-03-26 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2015146872A1 true WO2015146872A1 (ja) | 2015-10-01 |
Family
ID=54195386
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2015/058656 WO2015146872A1 (ja) | 2014-03-26 | 2015-03-23 | 酸素高炉の操業方法 |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP3124626B1 (ja) |
JP (1) | JP6229863B2 (ja) |
KR (1) | KR20160120334A (ja) |
CN (1) | CN106103746B (ja) |
WO (1) | WO2015146872A1 (ja) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2020020011A (ja) * | 2018-08-02 | 2020-02-06 | Jfeスチール株式会社 | 銑鉄製造設備およびそれを用いた銑鉄製造方法 |
CN111485044A (zh) * | 2019-01-29 | 2020-08-04 | 北京北大先锋科技有限公司 | 一种拟纯氧炼铁及高炉气循环利用方法及装置 |
JP2021152210A (ja) * | 2020-03-23 | 2021-09-30 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP2021152211A (ja) * | 2020-03-23 | 2021-09-30 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP2021152212A (ja) * | 2020-03-23 | 2021-09-30 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP2021175821A (ja) * | 2020-04-24 | 2021-11-04 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PL3425070T3 (pl) | 2017-07-03 | 2022-05-23 | L'air Liquide, Société Anonyme pour l'Étude et l'Exploitation des Procédés Georges Claude | Sposób eksploatacji zakładu wytwarzającego żelazo lub stal |
CN108103254B (zh) * | 2017-12-19 | 2019-07-09 | 武汉钢铁有限公司 | 基于低品质氧及大加湿的富氢高炉控制系统及方法 |
DE102018209042A1 (de) * | 2018-06-07 | 2019-12-12 | Thyssenkrupp Ag | Anlagenverbund zur Stahlerzeugung sowie ein Verfahren zum Betreiben des Anlagenverbundes. |
CN114787391B (zh) * | 2019-11-29 | 2023-09-12 | 日本制铁株式会社 | 高炉的操作方法 |
JP7028364B2 (ja) * | 2019-11-29 | 2022-03-02 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
EP4083234A4 (en) * | 2019-12-26 | 2023-07-05 | JFE Steel Corporation | BLAST FURNACE OPERATION METHOD AND AUXILIARY BLAST FURNACE EQUIPMENT |
KR20220082037A (ko) * | 2020-01-23 | 2022-06-16 | 제이에프이 스틸 가부시키가이샤 | 고로의 조업 방법 및 고로 부대 설비 |
KR20220129625A (ko) * | 2020-04-24 | 2022-09-23 | 제이에프이 스틸 가부시키가이샤 | 고로의 조업 방법 및 고로 부대 설비 |
WO2024047010A1 (en) * | 2022-08-29 | 2024-03-07 | Paul Wurth S.A. | Iron ore reducing and melting apparatus and method |
LU502718B1 (en) * | 2022-08-29 | 2024-02-29 | Wurth Paul Sa | Method for operating a smelting furnace installation |
WO2024047061A1 (en) * | 2022-08-29 | 2024-03-07 | Paul Wurth S.A. | Method for operating a smelting furnace installation |
LU502719B1 (en) * | 2022-08-29 | 2024-02-29 | Wurth Paul Sa | Method for operating a smelting furnace installation |
WO2024047062A1 (en) * | 2022-08-29 | 2024-03-07 | Paul Wurth S.A. | Method for operating a smelting furnace installation |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005213591A (ja) * | 2004-01-29 | 2005-08-11 | Jfe Steel Kk | 高炉への固体燃料吹き込み方法及び吹き込みランス |
JP2011202271A (ja) * | 2010-03-02 | 2011-10-13 | Jfe Steel Corp | 酸化炭素含有ガスの利用方法 |
JP2013010697A (ja) * | 2011-06-28 | 2013-01-17 | Jfe Steel Corp | 製鉄所発生ガスからのメタノールの製造方法及び高炉操業方法 |
JP2013019008A (ja) * | 2011-07-08 | 2013-01-31 | Jfe Steel Corp | 高炉操業方法 |
JP2013040402A (ja) * | 2011-07-15 | 2013-02-28 | Jfe Steel Corp | 高炉操業方法 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60159104A (ja) | 1984-01-27 | 1985-08-20 | Nippon Kokan Kk <Nkk> | 高炉操業方法 |
JPS6114290A (ja) | 1984-06-30 | 1986-01-22 | Nippon Kokan Kk <Nkk> | 石炭の乾留ガス化方法 |
JPS61124510A (ja) | 1984-11-21 | 1986-06-12 | Sumitomo Metal Ind Ltd | 高炉への燃料吹込み方法 |
JPS6227509A (ja) * | 1985-07-26 | 1987-02-05 | Nippon Kokan Kk <Nkk> | 高炉操業方法 |
JPS63171807A (ja) | 1987-01-09 | 1988-07-15 | Nkk Corp | 酸素高炉の操業方法 |
CN1216154C (zh) * | 2003-06-23 | 2005-08-24 | 安徽工业大学 | 一种高效低co2排放富氢燃气纯氧高炉炼铁工艺 |
-
2015
- 2015-03-23 EP EP15768555.3A patent/EP3124626B1/en active Active
- 2015-03-23 CN CN201580015653.XA patent/CN106103746B/zh active Active
- 2015-03-23 JP JP2016510317A patent/JP6229863B2/ja active Active
- 2015-03-23 WO PCT/JP2015/058656 patent/WO2015146872A1/ja active Application Filing
- 2015-03-23 KR KR1020167025284A patent/KR20160120334A/ko active Search and Examination
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005213591A (ja) * | 2004-01-29 | 2005-08-11 | Jfe Steel Kk | 高炉への固体燃料吹き込み方法及び吹き込みランス |
JP2011202271A (ja) * | 2010-03-02 | 2011-10-13 | Jfe Steel Corp | 酸化炭素含有ガスの利用方法 |
JP2013010697A (ja) * | 2011-06-28 | 2013-01-17 | Jfe Steel Corp | 製鉄所発生ガスからのメタノールの製造方法及び高炉操業方法 |
JP2013019008A (ja) * | 2011-07-08 | 2013-01-31 | Jfe Steel Corp | 高炉操業方法 |
JP2013040402A (ja) * | 2011-07-15 | 2013-02-28 | Jfe Steel Corp | 高炉操業方法 |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2020020011A (ja) * | 2018-08-02 | 2020-02-06 | Jfeスチール株式会社 | 銑鉄製造設備およびそれを用いた銑鉄製造方法 |
CN111485044A (zh) * | 2019-01-29 | 2020-08-04 | 北京北大先锋科技有限公司 | 一种拟纯氧炼铁及高炉气循环利用方法及装置 |
CN111485044B (zh) * | 2019-01-29 | 2023-10-10 | 北京北大先锋科技股份有限公司 | 一种拟纯氧炼铁及高炉气循环利用方法及装置 |
JP2021152210A (ja) * | 2020-03-23 | 2021-09-30 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP2021152211A (ja) * | 2020-03-23 | 2021-09-30 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP2021152212A (ja) * | 2020-03-23 | 2021-09-30 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP7192899B2 (ja) | 2020-03-23 | 2022-12-20 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP7192900B2 (ja) | 2020-03-23 | 2022-12-20 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP7192901B2 (ja) | 2020-03-23 | 2022-12-20 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP2021175821A (ja) * | 2020-04-24 | 2021-11-04 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
JP7192845B2 (ja) | 2020-04-24 | 2022-12-20 | Jfeスチール株式会社 | 高炉の操業方法および高炉附帯設備 |
Also Published As
Publication number | Publication date |
---|---|
JPWO2015146872A1 (ja) | 2017-04-13 |
EP3124626A1 (en) | 2017-02-01 |
CN106103746A (zh) | 2016-11-09 |
KR20160120334A (ko) | 2016-10-17 |
JP6229863B2 (ja) | 2017-11-15 |
EP3124626A4 (en) | 2017-04-19 |
CN106103746B (zh) | 2018-07-31 |
EP3124626B1 (en) | 2018-06-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6229863B2 (ja) | 酸素高炉の操業方法 | |
CN105899686A (zh) | 高炉的操作方法 | |
WO2017134829A1 (ja) | 高炉シャフト部への水素含有還元ガス供給方法 | |
JP6717629B2 (ja) | 高炉シャフト部への水素含有還元ガス供給方法 | |
JP6256710B2 (ja) | 酸素高炉の操業方法 | |
JP6354962B2 (ja) | 酸素高炉の操業方法 | |
KR101879895B1 (ko) | 용광로 스토브를 가열하기 위한 장치 및 방법 | |
WO2014189109A1 (ja) | 直接還元鉄の製造装置、及び直接還元鉄の製造方法 | |
JP6777894B2 (ja) | 酸素高炉設備およびその酸素高炉設備を用いた銑鉄の製造方法 | |
JP6098765B2 (ja) | 酸素高炉への微粉炭吹き込み方法 | |
JP2007138207A (ja) | 溶融還元方法 | |
KR20100082696A (ko) | 용광로에서의 철 제조방법 및 이 제조방법으로부터 얻어지는 상부 가스의 사용방법 | |
JP6922864B2 (ja) | 銑鉄製造設備およびそれを用いた銑鉄製造方法 | |
JP7055082B2 (ja) | 高炉の操業方法 | |
JP2015193927A (ja) | 酸素高炉の操業方法 | |
KR101751069B1 (ko) | 저등급 연료의 연소 방법 | |
JP6919632B2 (ja) | 銑鉄製造設備およびそれを用いた銑鉄製造方法 | |
EP4095268A1 (en) | Blast furnace operation method and auxiliary equipment for blast furnace | |
TWI758025B (zh) | 高爐之操作方法及高爐附帶設備 | |
CN103547863A (zh) | 用于处理含二氧化碳的废气的方法 | |
US20220380860A1 (en) | Method of operating blast furnace and blast furnace ancillary facility | |
JP2006328489A (ja) | 還元金属の製造方法 | |
JP2010150937A (ja) | ガスタービンコンバインド発電設備の運転方法及び製鉄所でのエネルギー運用方法 | |
TW202129015A (zh) | 高爐之操作方法及高爐附帶設備 | |
CN112944923A (zh) | 一种钢厂烧结烟气低成本协同处理超净排放工艺及系统 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 15768555 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 2016510317 Country of ref document: JP Kind code of ref document: A |
|
ENP | Entry into the national phase |
Ref document number: 20167025284 Country of ref document: KR Kind code of ref document: A |
|
REEP | Request for entry into the european phase |
Ref document number: 2015768555 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2015768555 Country of ref document: EP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |