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WO2025164232A1 - Method for blowing reducing gas into blast furnace and blast furnace - Google Patents

Method for blowing reducing gas into blast furnace and blast furnace

Info

Publication number
WO2025164232A1
WO2025164232A1 PCT/JP2025/000349 JP2025000349W WO2025164232A1 WO 2025164232 A1 WO2025164232 A1 WO 2025164232A1 JP 2025000349 W JP2025000349 W JP 2025000349W WO 2025164232 A1 WO2025164232 A1 WO 2025164232A1
Authority
WO
WIPO (PCT)
Prior art keywords
reducing gas
blast furnace
hot air
tuyere
height position
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
PCT/JP2025/000349
Other languages
French (fr)
Japanese (ja)
Inventor
良徳 松倉
尚 熊岡
公平 砂原
親司 上城
浩一 横山
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.)
Nippon Steel Corp
Original Assignee
Nippon 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP2025543364A priority Critical patent/JPWO2025164232A1/ja
Publication of WO2025164232A1 publication Critical patent/WO2025164232A1/en
Pending legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/16Tuyéres

Definitions

  • This application discloses a method for injecting reducing gas into a blast furnace and a blast furnace.
  • Patent Document 1 discloses a method in which a lance for injecting reducing gas is disposed in the hot blast flow path or wall surface of a hot blast tuyere, and reducing gas is injected through the lance.
  • Patent Document 2 discloses a method in which a fuel injection lance is inserted into the wall surface of a hot blast tuyere, and pulverized coal as fuel is injected into the blast furnace through the fuel injection lance.
  • Patent Document 1 When a lance is placed within the flow path of a hot blast tuyere, as disclosed in Patent Document 1, the lance is exposed to hot blast, raising concerns about thermal damage to the lance. Furthermore, when a reducing gas with a low specific gravity is injected into a blast furnace through a reducing gas injection lance attached to a hot blast tuyere, the reducing gas tends to rise along the wall of the blast furnace, resulting in uneven flow of the reducing gas. Prior art has not adequately considered the uneven flow of reducing gas within a blast furnace. This application discloses technology that can prevent thermal damage to the reducing gas injection lance and can prevent uneven flow of the reducing gas when a reducing gas with a low specific gravity is injected into the interior of a blast furnace.
  • a method for injecting reducing gas into a blast furnace comprising: Hot air is blown into the blast furnace from a hot air tuyere provided below the shaft lower end of the blast furnace and above the tap hole, Injecting a reducing gas into the blast furnace through a reducing gas injection lance that is provided within a wall surface of the hot blast tuyere and has an opening at a tip end of the hot blast tuyere,
  • the reducing gas is a gas that functions as a reducing agent inside the blast furnace,
  • the specific gravity of the reducing gas is smaller than the specific gravity of the hot air,
  • the height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
  • a method of injecting reducing gas into a blast furnace ⁇ Aspect 2> The method for injecting a reducing gas into a blast furnace according to aspect 1, The height position P1 is located below the height position P2 . A method of injecting reducing gas into a blast furnace. ⁇ Aspect 3> The method for injecting a reducing gas into a blast furnace according to aspect 1 or 2, The reducing gas comprises hydrogen gas. A method of injecting reducing gas into a blast furnace.
  • the height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
  • the blast furnace of aspect 4 The height position P1 is located below the height position P2 .
  • the technology disclosed herein makes it possible to prevent thermal damage to the reducing gas injection lance and to prevent the reduction gas from drifting when a reducing gas with a low specific gravity is injected into the interior of a blast furnace through the reducing gas injection lance.
  • 1 shows a schematic diagram of an example of the configuration of a blast furnace, with some components provided in the blast furnace omitted.
  • 10 is a schematic diagram showing another example of the configuration of the lance tip at the tip of the hot air tuyere.
  • 1 is a schematic diagram showing an example of the positional relationship between hot blast tuyere and reducing gas injection lance in a blast furnace.
  • 1 is a schematic diagram showing an example of the positional relationship between hot blast tuyere and reducing gas injection lance in a blast furnace.
  • 1 is a schematic diagram showing an example of the positional relationship between hot blast tuyere and reducing gas injection lance in a blast furnace.
  • the positional relationship between the hot blast tuyere and the lance opening for each of the preceding example, Examples 1 to 3, and Comparative Examples 1 and 2 is shown schematically.
  • a method for injecting reducing gas into a blast furnace 10 includes the steps of: Hot air is blown into the blast furnace 10 from a hot air tuyere 13 provided below the shaft lower end 11ax of the blast furnace 10 and above the tap hole 12, The method includes injecting a reducing gas into the inside of the blast furnace 10 from a reducing gas injection lance 14 that is provided within the wall surface of the hot blast tuyere 13 and has an opening 14a at the tip 13a of the hot blast tuyere 13.
  • the reducing gas is a gas that functions as a reducing agent inside the blast furnace 10 .
  • the specific gravity of the reducing gas is smaller than the specific gravity of the hot air.
  • the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is located below the height position P2 .
  • the blast furnace 10 has a hot blast tuyere 13 below the shaft lower end 11ax and above the tap hole 12.
  • the "shaft lower end” refers to the boundary between the shaft 11a and the belly 11b.
  • the “shaft” refers to the portion above the belly 11b, where the furnace diameter typically increases from top to bottom.
  • the “belly” refers to the portion below the shaft and above the bosch 11c, where the furnace diameter typically is greatest.
  • the furnace diameter (diameter) of the belly 11b may be, for example, 5 m or more and 20 m or less, or 10 m or more and 18 m or less.
  • the "tap hole” refers to a molten iron tap hole provided at the bottom of the blast furnace 10.
  • the "hot blast tuyere” refers to a nozzle for blowing hot air into the blast furnace.
  • the blast furnace 10 may have a hot air tuyere 13 below the belly lower end 11bx and above the tap hole 12, or may have a hot air tuyere 13 below the morning glory lower end 11cx and above the tap hole 12.
  • the configuration of the hot air tuyere 13 is known.
  • the hot air tuyere 13 may have a water-cooled structure.
  • the hot air tuyere 13 may be connected to a hot air stove outside the blast furnace 10 via a hot air pipe or the like.
  • the blast furnace 10 may be configured so that hot air is blown into the interior of the blast furnace 10 from the hot air stove via the hot air pipe and the hot air tuyere 13.
  • the diameter of the hot air tuyere 13 (the circle-equivalent diameter of the opening facing the interior of the blast furnace 10, the nozzle diameter) may be, for example, 20 mm or more and 400 mm or less, or 40 mm or more and 300 mm or less.
  • the number of hot air tuyere 13 provided in the blast furnace 10 is not particularly limited and can be determined according to the internal volume of the blast furnace.
  • a plurality of hot air tuyere 13 can be arranged in the circumferential direction of the blast furnace 10.
  • a plurality of hot air tuyere 13 can be arranged in the circumferential direction when viewed from above.
  • the height position P2 of the center of each of the plurality of hot air tuyere 13 is the same.
  • the blast furnace 10 has a reducing gas injection lance 14.
  • the reducing gas injection lance 14 can be connected to a reducing gas supply source outside the blast furnace 10 via a reducing gas supply passage or the like.
  • the blast furnace 10 can be configured so that reducing gas is injected from the reducing gas supply source into the interior of the blast furnace 10 via the reducing gas supply passage and the reducing gas injection lance 14.
  • the reducing gas injection lance 14 is provided within the wall surface of the hot air tuyere 13.
  • a "reducing gas injection lance provided within the wall surface of the hot air tuyere” does not necessarily have to be embedded within the wall surface of the hot air tuyere all the way to the tip of the lance, as shown in FIG. 1. It also includes, for example, a configuration in which at least a portion of the lance is exposed within the flow path of the hot air tuyere while contacting the inside of the wall surface of the hot air tuyere, as shown in FIG. 2.
  • the entire circumference of the reducing gas injection lance may be exposed within the flow path of the hot air tuyere. From the perspective of further suppressing thermal damage to the reducing gas injection lance, it is preferable that the entire circumference of the reducing gas injection lance be provided within the wall surface of the hot air tuyere.
  • the reducing gas injection lance 14 has an opening 14a at the tip 13a of the hot air tuyere 13, and is configured so that reducing gas is injected into the blast furnace 10 through the opening 14a.
  • a reducing gas injection lance having an opening at the tip of the hot air tuyere means that the reducing gas injection lance opens at or near the tip of the hot air tuyere.
  • the tip surface of the hot air tuyere and the lance opening do not need to be flush with each other (i.e., the tip of the lance does not need to reach the tip of the hot air tuyere).
  • "having an opening at the tip of the hot air tuyere” includes not only a configuration in which the tip surface of the hot air tuyere and the lance opening are flush with each other (i.e., the tip of the lance reaches the tip of the hot air tuyere), but also a configuration in which the tip of the lance reaches near the tip of the hot air tuyere.
  • a lance is considered to have an "opening at the tip of the hot air tuyere" when the distance from the tip of the lance to the tip of the hot air tuyere is 0 mm or more and 50 mm or less.
  • the reducing gas injection lance 14 by providing the reducing gas injection lance 14 within the wall surface of the hot air tuyere 13, the reducing gas injection lance 14 is less likely to be exposed to hot air, and even if it is exposed to hot air, the reducing gas injection lance 14 can be cooled by the water-cooling structure within the wall surface of the hot air tuyere 13, thereby suppressing thermal damage to the reducing gas injection lance 14.
  • the diameter of the opening 14a of the reducing gas injection lance 14 (the circular equivalent diameter of the opening facing the inside of the blast furnace 10) may be, for example, 10 mm or more and 50 mm or less, or 20 mm or more and 30 mm or less.
  • the diameter of the opening 14a of the reducing gas injection lance 14 may be 0.05% or more and 0.8% or less, or 0.1% or more and 0.5% or less, of the diameter of the hot air tuyere 13.
  • the number of reducing gas injection lances 14 provided in the blast furnace 10 is not particularly limited.
  • at least one reducing gas injection lance 14 may be provided in at least one hot blast tuyere 13 provided in the blast furnace 10.
  • only some of the plurality of hot blast tuyere 13 may have reducing gas injection lances 14, or all of the plurality of hot blast tuyere 13 may have reducing gas injection lances 14.
  • one reducing gas injection lance 14 may be provided for one hot blast tuyere 13, or multiple reducing gas injection lances 14 may be provided.
  • the height positions P1 of the centers of the openings 14a of the multiple reducing gas injection lances 14 may be the same as or different from each other.
  • the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is lower than the height position P2 . According to new findings by the inventors, if the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is higher than the height position P2 of the center of the hot blast tuyere 13, the reducing gas injected from the reducing gas injection lance 14 will rise along the wall surface of the blast furnace 10, and the reducing gas will likely flow unevenly inside the blast furnace 10.
  • the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is lower than the height position P2 , the amount of reducing gas flowing below the hot blast inside the blast furnace 10 increases, and the amount of reducing gas rising along the wall surface decreases, making it easier for the reducing gas to reach the radial center (furnace center) inside the blast furnace 10.
  • uneven flow of the reducing gas inside the blast furnace 10 is suppressed, and the utilization efficiency of the reducing gas is improved.
  • the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is lower than the height position P2 of the center of the hot blast tuyere 13, the effect of suppressing uneven flow of the reducing gas becomes more remarkable.
  • 3A and 3B show an example in which the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is lower than the height position P2 of the center of the hot blast tuyere 13.
  • the center of the opening 14a of the reducing gas injection lance 14 may be located directly below the center of the hot blast tuyere 13. That is, the position of the center of the opening 14a of the reducing gas injection lance 14 in the circumferential direction of the blast furnace 10 may be the same as the position of the center of the hot blast tuyere 13.
  • FIG. 3A shows an example in which the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is lower than the height position P2 of the center of the hot blast tuyere 13.
  • the center of the opening 14a of the reducing gas injection lance 14 may be located obliquely below the center of the hot blast tuyere 13. That is, the center of the opening 14a of the reducing gas injection lance 14 may be located at a position different from the center of the hot blast tuyere 13 in the circumferential direction of the blast furnace 10.
  • 3C shows a case where the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13. As shown in FIG. 3C, the opening 14a of the reducing gas injection lance 14 may be provided beside the hot blast tuyere 13.
  • the hot air blown from the hot air tuyere 13 may be, for example, air or oxygen-enriched air.
  • the temperature of the hot air is, for example, 1000°C or higher.
  • the temperature of the hot air may be 1000°C or higher and 2000°C or lower, 1000°C or higher and 1700°C or lower, 1000°C or higher and 1500°C or lower, or 1000°C or higher and 1300°C or lower.
  • the flow rate of the hot air in the hot air tuyere 13 (flow rate of hot air ( m3 /s)/opening area of the outlet of the hot air tuyere 13 ( m2 )) may be adjusted depending on the operating status of the blast furnace 10. In one embodiment, the flow rate of the hot air may be a flow rate V1 described later.
  • the reducing gas injected from the reducing gas injection lance 14 functions as a reducing agent inside the blast furnace 10.
  • the term "reducing gas” as used herein is included as long as it can generate a reducing agent (reducing component) inside the blast furnace 10 by thermal decomposition or the like.
  • the specific gravity of the reducing gas is lower than the specific gravity of the hot air injected into the blast furnace 10 from the hot air tuyere 13.
  • Examples of such reducing gas include at least one selected from hydrogen gas, hydrocarbon gas (e.g., methane gas), carbon monoxide gas, and ammonia gas.
  • the temperature of the reducing gas injected from the reducing gas injection lance 14 may be, for example, 0°C or higher and 2000°C or lower, or 25°C or higher and 1500°C or lower.
  • the flow velocity of the reducing gas at the opening 14a of the reducing gas injection lance 14 (flow rate of reducing gas ( m3 /s)/opening area of the outlet of the reducing gas injection lance 14 ( m2 )) may be, for example, equal to or less than the sonic velocity at the operating temperature of each reducing gas.
  • the flow velocity of the reducing gas injected from the reducing gas injection lance 14 may be flow velocity V2, which will be described later.
  • the flow velocity V1 of the hot air blown from the hot air tuyere 13 is not particularly limited, but for example, if the flow velocity V1 is 100 m/s or more and 1000 m/s or less, and particularly 200 m/s or more and 400 m/s or less, uneven flow of the reducing gas inside the blast furnace 10 is more likely to be suppressed.
  • the flow velocity V2 of the reducing gas blown from the reducing gas injection lance 14 is not particularly limited, but for example, if the flow velocity V2 is 100 m/s or more and 1000 m/s or less, and particularly 200 m/s or more and 800 m/s or less, ventilation inside the blast furnace 10 is stable, resulting in operation in which the reduction reaction inside the furnace proceeds stably.
  • gases may be injected together with the reducing gas from the reducing gas injection lance 14.
  • gases include inert gases such as nitrogen gas.
  • a blast furnace 10 includes: A hot blast tuyere 13 provided below the shaft lower end 11ax of the blast furnace 10 and above the tap hole 12; and a reducing gas injection lance 14 provided within the wall surface of the hot blast tuyere 13 and having an opening 14 a at the tip 13 a of the hot blast tuyere 13 .
  • the reducing gas injected into the inside of the blast furnace 10 from the reducing gas injection lance 14 is a gas that functions as a reducing agent inside the blast furnace 10 .
  • the specific gravity of the reducing gas is smaller than the specific gravity of the hot air blown into the inside of the blast furnace 10 from the hot air tuyere 13 .
  • the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is located below the height position P2 .
  • the effect of suppressing the uneven flow of the reducing gas is further enhanced when the height position P1 is located below the height position P2 in the blast furnace 10. Furthermore, it is considered that the effect of the technology of the present disclosure is further enhanced when the reducing gas contains hydrogen gas.
  • the molten iron is tapped from a tap hole 12 provided at the bottom of the blast furnace 10.
  • the amount of carbon-containing reducing material used such as coke
  • the blast furnace 10 can have various configurations as long as it is capable of producing pig iron as described above.
  • the blast furnace 10 may have other tuyere(s) and lance(s) in addition to the above-described hot blast tuyere(s) 13 and reducing gas injection lance(s) 14.
  • blast furnace 10 other reducing gas injection lance(s) may be present above the hot blast tuyere(s) 13.
  • the configuration of the blast furnace 10 other than the hot blast tuyere(s) 13 and reducing gas injection lance(s) 14 is known in the art, and therefore will not be described in detail here.
  • thermal damage to the reducing gas injection lance 14 can be suppressed by providing the reducing gas injection lance 14 within the wall surface of the hot blast tuyere 13.
  • the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is lower than the height position P2 , so that uneven flow of the reducing gas inside the blast furnace 10 can be suppressed.
  • the lance was inserted into the hot air flow path of the hot air tuyere (outside the wall surface) so that the center of the opening at the tip of the lance was positioned at the center of the opening of the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.
  • Example 1 As shown in "Example 1" in Figure 4, a lance was inserted into the wall of the hot air tuyere so that the center of the opening at the tip of the lance was positioned directly below the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.
  • Example 2 As shown in "Example 2" in Figure 4, a lance was inserted into the wall of the hot air tuyere so that the center of the opening at the tip of the lance was positioned diagonally below the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.
  • Example 3 As shown in "Example 3" in Figure 4, a lance was inserted into the wall surface of the hot air tuyere so that the height position of the center of the opening at the tip of the lance was the same as the height position of the center of the opening in the hot air tuyere. Hot air was blown from the hot air tuyere, and hydrogen gas was blown from the lance.
  • Comparative Example 1 As shown in "Comparative Example 1" in Figure 4, a lance was inserted into the wall of the hot air tuyere so that the center of the opening at the tip of the lance was positioned diagonally above the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.
  • Comparative Example 2 As shown in "Comparative Example 2" in Figure 4, a lance was inserted into the wall surface of the hot air tuyere so that the center of the opening at the tip of the lance was positioned directly above the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.
  • the prior art example has issues with the durability of the lance.
  • this issue can be resolved by arranging the reducing gas injection lance within the wall surface of the hot blast tuyere (with at least a portion of the entire circumference of the lance positioned inside the wall surface of the hot blast tuyere), as in Examples 1 to 3.
  • Examples 1 to 3 are more advantageous than the prior art.
  • a method for injecting reducing gas into a blast furnace comprising: Hot air is blown into the blast furnace from a hot air tuyere provided below the shaft lower end of the blast furnace and above the tap hole, Injecting a reducing gas into the blast furnace through a reducing gas injection lance that is provided within a wall surface of the hot blast tuyere and has an opening at a tip end of the hot blast tuyere,
  • the reducing gas is a gas that functions as a reducing agent inside the blast furnace,
  • the specific gravity of the reducing gas is smaller than the specific gravity of the hot air,
  • the height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
  • the height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .

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

Abstract

Disclosed is a method by which it is possible to suppress drift of a reducing gas when a reducing gas having a low specific gravity is blown into the interior of a blast furnace. A method for blowing a reducing gas into a blast furnace according to the present disclosure comprises: blowing hot air into the interior of the blast furnace from a hot air tuyere provided below the lower end of the shaft of the blast furnace and above a tap hole; and blowing the reducing gas into the interior of the blast furnace through a reducing gas blowing lance that is provided in the wall surface of the hot air tuyere and that has an opening at the tip end of the hot air tuyere. The reducing gas functions as a reducing material in the interior of the blast furnace, and the specific gravity of the reducing gas is lower than the specific gravity of the hot air. The height position P1 of the center of the opening of the reducing gas blowing lance is the same as the height position P2 of the center of the hot air tuyere, or is below the height position P2.

Description

高炉への還元ガス吹込方法及び高炉Method for injecting reducing gas into blast furnace and blast furnace

 本願は高炉への還元ガス吹込方法及び高炉を開示する。 This application discloses a method for injecting reducing gas into a blast furnace and a blast furnace.

 製鉄プロセスにおいてCO排出量を削減することが検討されている。例えば、高炉にて銑鉄を製造する際、還元材としてのコークス等の一部に替えて、水素ガス等の還元ガスを利用することがあり得る。高炉への還元ガス吹込方法として、特許文献1には、熱風羽口の熱風流路内又は壁面内に還元ガス吹込用のランスを配置し、当該ランスを介して還元ガスを吹き込む方法が開示されている。尚、還元ガスの吹き込みを想定したものではないが、特許文献2には、熱風羽口の壁面内に燃料噴射ランスを挿入し、当該燃料噴射ランスを介して高炉内へと燃料としての粉炭を吹き込む方法が開示されている。 Reducing CO2 emissions in the steelmaking process has been studied. For example, when producing pig iron in a blast furnace, a reducing gas such as hydrogen gas may be used in place of a portion of the reducing material, such as coke. As a method for injecting reducing gas into a blast furnace, Patent Document 1 discloses a method in which a lance for injecting reducing gas is disposed in the hot blast flow path or wall surface of a hot blast tuyere, and reducing gas is injected through the lance. Although not intended to inject reducing gas, Patent Document 2 discloses a method in which a fuel injection lance is inserted into the wall surface of a hot blast tuyere, and pulverized coal as fuel is injected into the blast furnace through the fuel injection lance.

特許第4997734号公報Patent No. 4997734 特許第5840202号公報Patent No. 5840202

 特許文献1に開示されているように熱風羽口の流路内にランスを配置した場合、ランスが熱風に曝され、ランスの熱損傷等が懸念される。また、熱風羽口に設けられた還元ガス吹込ランスを介して高炉内へと比重の小さな還元ガスを吹き込む場合、高炉内の壁面を伝って還元ガスが上昇するなどして、還元ガスの偏流が生じ易い。従来技術においては、高炉内の還元ガスの偏流について、十分な検討がなされていない。本願は、高炉の内部へと比重の小さな還元ガスを吹き込む場合に、還元ガス吹込ランスの熱損傷を抑制可能であり、かつ、還元ガスの偏流を抑制可能な技術を開示する。 When a lance is placed within the flow path of a hot blast tuyere, as disclosed in Patent Document 1, the lance is exposed to hot blast, raising concerns about thermal damage to the lance. Furthermore, when a reducing gas with a low specific gravity is injected into a blast furnace through a reducing gas injection lance attached to a hot blast tuyere, the reducing gas tends to rise along the wall of the blast furnace, resulting in uneven flow of the reducing gas. Prior art has not adequately considered the uneven flow of reducing gas within a blast furnace. This application discloses technology that can prevent thermal damage to the reducing gas injection lance and can prevent uneven flow of the reducing gas when a reducing gas with a low specific gravity is injected into the interior of a blast furnace.

 本願は、上記課題を解決するための手段として、以下の複数の態様を開示する。
<態様1>
 高炉への還元ガス吹込方法であって、
  前記高炉のシャフト下端よりも下方かつ出銑口よりも上方に設けられた熱風羽口から、前記高炉の内部へと、熱風を吹き込むとともに、
  前記熱風羽口の壁面内に設けられ、かつ、前記熱風羽口の先端部に開口を有する還元ガス吹込ランスを介して、前記高炉の内部へと、還元ガスを吹き込むこと、を含み、
  前記還元ガスが、前記高炉の内部において還元材として機能するガスであり、
  前記還元ガスの比重が、前記熱風の比重よりも小さく、
  前記還元ガス吹込ランスの前記開口の中心の高さ位置Pが、前記熱風羽口の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する、
 高炉への還元ガス吹込方法。
<態様2>
 態様1の高炉への還元ガス吹込方法であって、
  前記高さ位置Pが、前記高さ位置Pよりも下方に存在する、
 高炉への還元ガス吹込方法。
<態様3>
 態様1又は2の高炉への還元ガス吹込方法であって、
  前記還元ガスが、水素ガスを含む、
 高炉への還元ガス吹込方法。
<態様4>
 高炉であって、
  前記高炉のシャフト下端よりも下方かつ出銑口よりも上方に設けられた熱風羽口と、
  前記熱風羽口の壁面内に設けられ、かつ、前記熱風羽口の先端部に開口を有する還元ガス吹込ランスと、
 を有し、
  前記還元ガス吹込ランスから前記高炉の内部へと吹き込まれる還元ガスが、前記高炉の内部において還元材として機能するガスであり、
  前記還元ガスの比重が、前記熱風羽口から前記高炉の内部へと吹き込まれる熱風の比重よりも小さく、
  前記還元ガス吹込ランスの前記開口の中心の高さ位置Pが、前記熱風羽口の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する、
 高炉。
<態様5>
 態様4の高炉であって、
  前記高さ位置Pが、前記高さ位置Pよりも下方に存在する、
 高炉。
<態様6>
 態様4又は5の高炉であって、
  前記還元ガスが、水素ガスを含む、
 高炉。
The present application discloses the following aspects as means for solving the above problems.
<Aspect 1>
A method for injecting reducing gas into a blast furnace, comprising:
Hot air is blown into the blast furnace from a hot air tuyere provided below the shaft lower end of the blast furnace and above the tap hole,
Injecting a reducing gas into the blast furnace through a reducing gas injection lance that is provided within a wall surface of the hot blast tuyere and has an opening at a tip end of the hot blast tuyere,
The reducing gas is a gas that functions as a reducing agent inside the blast furnace,
The specific gravity of the reducing gas is smaller than the specific gravity of the hot air,
The height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
A method of injecting reducing gas into a blast furnace.
<Aspect 2>
The method for injecting a reducing gas into a blast furnace according to aspect 1,
The height position P1 is located below the height position P2 .
A method of injecting reducing gas into a blast furnace.
<Aspect 3>
The method for injecting a reducing gas into a blast furnace according to aspect 1 or 2,
The reducing gas comprises hydrogen gas.
A method of injecting reducing gas into a blast furnace.
<Aspect 4>
A blast furnace,
a hot blast tuyere provided below the shaft lower end of the blast furnace and above the tap hole;
a reducing gas injection lance provided within a wall surface of the hot air tuyere and having an opening at a tip end of the hot air tuyere;
and
the reducing gas injected from the reducing gas injection lance into the inside of the blast furnace is a gas that functions as a reducing agent inside the blast furnace,
the specific gravity of the reducing gas is lower than the specific gravity of the hot air blown into the inside of the blast furnace from the hot air tuyere,
The height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
Blast furnace.
<Aspect 5>
5. The blast furnace of aspect 4,
The height position P1 is located below the height position P2 .
Blast furnace.
<Aspect 6>
The blast furnace of aspect 4 or 5,
The reducing gas comprises hydrogen gas.
Blast furnace.

 本開示の技術によれば、還元ガス吹込ランスを介して高炉の内部へと比重の小さな還元ガスを吹き込む場合に、還元ガス吹込ランスの熱損傷を抑制可能であり、かつ、還元ガスの偏流を抑制可能である。 The technology disclosed herein makes it possible to prevent thermal damage to the reducing gas injection lance and to prevent the reduction gas from drifting when a reducing gas with a low specific gravity is injected into the interior of a blast furnace through the reducing gas injection lance.

高炉の構成の一例を概略的に示している。高炉に備えられる一部の構成については省略して示している。1 shows a schematic diagram of an example of the configuration of a blast furnace, with some components provided in the blast furnace omitted. 熱風羽口の先端部におけるランス先端部の構成の他の例を概略的に示している。10 is a schematic diagram showing another example of the configuration of the lance tip at the tip of the hot air tuyere. 高炉における熱風羽口と還元ガス吹込ランスとの位置関係の一例を概略的に示している。1 is a schematic diagram showing an example of the positional relationship between hot blast tuyere and reducing gas injection lance in a blast furnace. 高炉における熱風羽口と還元ガス吹込ランスとの位置関係の一例を概略的に示している。1 is a schematic diagram showing an example of the positional relationship between hot blast tuyere and reducing gas injection lance in a blast furnace. 高炉における熱風羽口と還元ガス吹込ランスとの位置関係の一例を概略的に示している。1 is a schematic diagram showing an example of the positional relationship between hot blast tuyere and reducing gas injection lance in a blast furnace. 先行例、実施例1~3及び比較例1~2の各々についての熱風羽口とランス開口との位置関係を概略的に示している。The positional relationship between the hot blast tuyere and the lance opening for each of the preceding example, Examples 1 to 3, and Comparative Examples 1 and 2 is shown schematically.

 以下、本開示の高炉への還元ガス吹込方法及び高炉の一実施形態について説明する。ただし、本開示の高炉への還元ガス吹込方法及び高炉は以下の実施形態に限定されるものではない。 Below, one embodiment of the method for injecting reducing gas into a blast furnace and the blast furnace disclosed herein will be described. However, the method for injecting reducing gas into a blast furnace and the blast furnace disclosed herein are not limited to the following embodiment.

1.高炉への還元ガス吹込方法
 図1に示されるように、一実施形態に係る高炉10への還元ガス吹込方法は、
  前記高炉10のシャフト下端11axよりも下方かつ出銑口12よりも上方に設けられた熱風羽口13から、前記高炉10の内部へと、熱風を吹き込むとともに、
  前記熱風羽口13の壁面内に設けられ、かつ、前記熱風羽口13の先端部13aに開口14aを有する還元ガス吹込ランス14から、前記高炉10の内部へと、還元ガスを吹き込むこと、を含む。
  前記還元ガスは、前記高炉10の内部において還元材として機能するガスである。
  前記還元ガスの比重は、前記熱風の比重よりも小さい。
  前記還元ガス吹込ランス14の前記開口14aの中心の高さ位置Pは、前記熱風羽口13の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する。
1. Method for Injecting Reducing Gas into Blast Furnace As shown in FIG. 1, a method for injecting reducing gas into a blast furnace 10 according to one embodiment includes the steps of:
Hot air is blown into the blast furnace 10 from a hot air tuyere 13 provided below the shaft lower end 11ax of the blast furnace 10 and above the tap hole 12,
The method includes injecting a reducing gas into the inside of the blast furnace 10 from a reducing gas injection lance 14 that is provided within the wall surface of the hot blast tuyere 13 and has an opening 14a at the tip 13a of the hot blast tuyere 13.
The reducing gas is a gas that functions as a reducing agent inside the blast furnace 10 .
The specific gravity of the reducing gas is smaller than the specific gravity of the hot air.
The height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is located below the height position P2 .

1.1 熱風羽口
 高炉10は、シャフト下端11axよりも下方かつ出銑口12よりも上方に熱風羽口13を有する。「シャフト下端」とは、シャフト11aと炉腹(ベリー)11bとの境界部分をいう。「シャフト」とは、炉腹11bよりも上方の部分であって、通常、上から下に向かうにつれて炉径が増大する部分をいう。「炉腹」とは、シャフトよりも下方かつ朝顔(ボッシュ)11cよりも上方の部分であって、通常、炉径が最大となる部分をいう。炉腹11bの炉径(直径)は、例えば、5m以上20m以下、又は、10m以上18m以下であってもよい。「出銑口」とは、高炉10の下部に設けられた溶銑出湯口をいう。「熱風羽口」とは、高炉に熱風を吹き込むためのノズルをいう。高炉10は、炉腹下端11bxよりも下方かつ出銑口12よりも上方に熱風羽口13を有していてもよく、朝顔下端11cxよりも下方かつ出銑口12よりも上方に熱風羽口13を有していてもよい。
1.1 Hot Blast Tuyere The blast furnace 10 has a hot blast tuyere 13 below the shaft lower end 11ax and above the tap hole 12. The "shaft lower end" refers to the boundary between the shaft 11a and the belly 11b. The "shaft" refers to the portion above the belly 11b, where the furnace diameter typically increases from top to bottom. The "belly" refers to the portion below the shaft and above the bosch 11c, where the furnace diameter typically is greatest. The furnace diameter (diameter) of the belly 11b may be, for example, 5 m or more and 20 m or less, or 10 m or more and 18 m or less. The "tap hole" refers to a molten iron tap hole provided at the bottom of the blast furnace 10. The "hot blast tuyere" refers to a nozzle for blowing hot air into the blast furnace. The blast furnace 10 may have a hot air tuyere 13 below the belly lower end 11bx and above the tap hole 12, or may have a hot air tuyere 13 below the morning glory lower end 11cx and above the tap hole 12.

 熱風羽口13の構成は公知である。例えば、熱風羽口13は、水冷構造を有するものであってもよい。熱風羽口13は、高炉10の外部の熱風炉に対して、熱風管等を介して接続され得る。言い換えれば、高炉10は、熱風炉から熱風管及び熱風羽口13を介して、高炉10の内部に熱風が吹き込まれるように構成され得る。熱風羽口13の直径(高炉10の内部に面する開口の円相当直径、ノズル径)は、例えば、20mm以上400mm以下、又は、40mm以上300mm以下であってもよい。 The configuration of the hot air tuyere 13 is known. For example, the hot air tuyere 13 may have a water-cooled structure. The hot air tuyere 13 may be connected to a hot air stove outside the blast furnace 10 via a hot air pipe or the like. In other words, the blast furnace 10 may be configured so that hot air is blown into the interior of the blast furnace 10 from the hot air stove via the hot air pipe and the hot air tuyere 13. The diameter of the hot air tuyere 13 (the circle-equivalent diameter of the opening facing the interior of the blast furnace 10, the nozzle diameter) may be, for example, 20 mm or more and 400 mm or less, or 40 mm or more and 300 mm or less.

 高炉10に設けられる熱風羽口13の数は、特に限定されるものではなく、高炉の内容積に応じて、決定され得る。高炉10には、複数の熱風羽口13が高炉10の周方向に配置され得る。言い換えれば、高炉10においては、上面視において、複数の熱風羽口13が、円周方向上に配置され得る。通常、複数の熱風羽口13の各々の中心の高さ位置Pは、同様である。 The number of hot air tuyere 13 provided in the blast furnace 10 is not particularly limited and can be determined according to the internal volume of the blast furnace. In the blast furnace 10, a plurality of hot air tuyere 13 can be arranged in the circumferential direction of the blast furnace 10. In other words, in the blast furnace 10, a plurality of hot air tuyere 13 can be arranged in the circumferential direction when viewed from above. Usually, the height position P2 of the center of each of the plurality of hot air tuyere 13 is the same.

1.2 還元ガス吹込ランス
 高炉10は、還元ガス吹込ランス14を有する。還元ガス吹込ランス14は、高炉10の外部の還元ガス供給源に対して、還元ガス供給流路等を介して接続され得る。言い換えれば、高炉10は、還元ガス供給源から還元ガス供給流路及び還元ガス吹込ランス14を介して高炉10の内部に還元ガスが吹き込まれるように構成され得る。還元ガス供給源や還元ガス供給流路の形態に特に制限はない。
1.2 Reducing Gas Injection Lance The blast furnace 10 has a reducing gas injection lance 14. The reducing gas injection lance 14 can be connected to a reducing gas supply source outside the blast furnace 10 via a reducing gas supply passage or the like. In other words, the blast furnace 10 can be configured so that reducing gas is injected from the reducing gas supply source into the interior of the blast furnace 10 via the reducing gas supply passage and the reducing gas injection lance 14. There are no particular limitations on the configuration of the reducing gas supply source or the reducing gas supply passage.

 本実施形態においては、還元ガス吹込ランス14が、熱風羽口13の壁面内に設けられることが重要である。「熱風羽口の壁面内に設けられた還元ガス吹込ランス」とは、図1に示されるようにランス先端に至るまで熱風羽口の壁面内に埋設されている必要はなく、例えば、図2に示されるように、ランスの少なくとも一部が熱風羽口の壁面よりも内側に接しつつ熱風羽口の流路内に露出するような形態も含まれる。すなわち、還元ガス吹込ランスは、ランス全周のうちの少なくとも一部が、熱風羽口の壁面よりも内側に存在するなどして、熱風羽口内の水冷構造によって還元ガス吹込ランスの冷却が可能である限り(ランスの熱損傷が抑制され得る限り)、当該ランスの全周のうちの一部が熱風羽口の流路内に露出していてもよい。還元ガス吹込ランスの熱損傷をより一層抑制する観点からは、熱風羽口において、還元ガス吹込ランスの全周が当該熱風羽口の壁面内に設けられることが好ましい。また、本実施形態においては、還元ガス吹込ランス14が、熱風羽口13の先端部13aに開口14aを有し、当該開口14aから高炉10の内部へと還元ガスが吹き込まれるように構成される。「熱風羽口の先端部に開口を有する還元ガス吹込ランス」とは、還元ガス吹込ランスが、熱風羽口の先端又はその近傍において開口していることを意味する。本実施形態においては、熱風羽口の先端面とランス開口とが面一である(ランスの先端が熱風羽口の先端にまで達している)必要はない。すなわち、「熱風羽口の先端部に開口を有する」とは、熱風羽口の先端面とランス開口とが面一である(ランスの先端が熱風羽口の先端にまで達している)形態のほか、ランス先端が熱風羽口の先端の近傍にまで達している形態も含む。具体的には、ランス先端から熱風羽口の先端までの距離が、0mm以上50mm以下である場合に、ランスが「熱風羽口の先端部に開口を有する」ものとみなす。このように、本実施形態においては、還元ガス吹込ランス14が、熱風羽口13の壁面内に設けられることで、還元ガス吹込ランス14が熱風に曝され難くなり、また、熱風に曝されたとしても熱風羽口13の壁面内の水冷構造によって還元ガス吹込ランス14を冷却することができ、還元ガス吹込ランス14の熱損傷等が抑制され得る。 In this embodiment, it is important that the reducing gas injection lance 14 is provided within the wall surface of the hot air tuyere 13. A "reducing gas injection lance provided within the wall surface of the hot air tuyere" does not necessarily have to be embedded within the wall surface of the hot air tuyere all the way to the tip of the lance, as shown in FIG. 1. It also includes, for example, a configuration in which at least a portion of the lance is exposed within the flow path of the hot air tuyere while contacting the inside of the wall surface of the hot air tuyere, as shown in FIG. 2. In other words, as long as at least a portion of the entire circumference of the reducing gas injection lance is located inside the wall surface of the hot air tuyere, and the reducing gas injection lance can be cooled by the water-cooling structure within the hot air tuyere (as long as thermal damage to the lance can be suppressed), a portion of the entire circumference of the lance may be exposed within the flow path of the hot air tuyere. From the perspective of further suppressing thermal damage to the reducing gas injection lance, it is preferable that the entire circumference of the reducing gas injection lance be provided within the wall surface of the hot air tuyere. In this embodiment, the reducing gas injection lance 14 has an opening 14a at the tip 13a of the hot air tuyere 13, and is configured so that reducing gas is injected into the blast furnace 10 through the opening 14a. The phrase "a reducing gas injection lance having an opening at the tip of the hot air tuyere" means that the reducing gas injection lance opens at or near the tip of the hot air tuyere. In this embodiment, the tip surface of the hot air tuyere and the lance opening do not need to be flush with each other (i.e., the tip of the lance does not need to reach the tip of the hot air tuyere). That is, "having an opening at the tip of the hot air tuyere" includes not only a configuration in which the tip surface of the hot air tuyere and the lance opening are flush with each other (i.e., the tip of the lance reaches the tip of the hot air tuyere), but also a configuration in which the tip of the lance reaches near the tip of the hot air tuyere. Specifically, a lance is considered to have an "opening at the tip of the hot air tuyere" when the distance from the tip of the lance to the tip of the hot air tuyere is 0 mm or more and 50 mm or less. In this manner, in this embodiment, by providing the reducing gas injection lance 14 within the wall surface of the hot air tuyere 13, the reducing gas injection lance 14 is less likely to be exposed to hot air, and even if it is exposed to hot air, the reducing gas injection lance 14 can be cooled by the water-cooling structure within the wall surface of the hot air tuyere 13, thereby suppressing thermal damage to the reducing gas injection lance 14.

 還元ガス吹込ランス14の開口14aの直径(高炉10の内部に面する開口の円相当直径)は、例えば、10mm以上50mm以下であってもよく、20mm以上30mm以下であってもよい。或いは、還元ガス吹込ランス14の開口14aの直径は、熱風羽口13の直径の0.05%以上0.8%以下、又は、0.1%以上0.5%以下であってもよい。 The diameter of the opening 14a of the reducing gas injection lance 14 (the circular equivalent diameter of the opening facing the inside of the blast furnace 10) may be, for example, 10 mm or more and 50 mm or less, or 20 mm or more and 30 mm or less. Alternatively, the diameter of the opening 14a of the reducing gas injection lance 14 may be 0.05% or more and 0.8% or less, or 0.1% or more and 0.5% or less, of the diameter of the hot air tuyere 13.

 高炉10に設けられる還元ガス吹込ランス14の数は、特に限定されるものではない。例えば、高炉10に設けられる少なくとも1つの熱風羽口13に、少なくとも1つの還元ガス吹込ランス14が設けられていてもよい。言い換えれば、高炉10が複数の熱風羽口13を有する場合、当該複数の熱風羽口13の一部のみが還元ガス吹込ランス14を有していてもよいし、その全部が還元ガス吹込ランス14を有していてもよい。また、1つの熱風羽口13に対して、1つの還元ガス吹込ランス14が設けられていてもよいし、複数の還元ガス吹込ランス14が設けられていてもよい。複数の還元ガス吹込ランス14の各々の開口14aの中心の高さ位置Pは、互いに同じであってもよいし、互いに異なっていてもよい。 The number of reducing gas injection lances 14 provided in the blast furnace 10 is not particularly limited. For example, at least one reducing gas injection lance 14 may be provided in at least one hot blast tuyere 13 provided in the blast furnace 10. In other words, when the blast furnace 10 has a plurality of hot blast tuyere 13, only some of the plurality of hot blast tuyere 13 may have reducing gas injection lances 14, or all of the plurality of hot blast tuyere 13 may have reducing gas injection lances 14. Furthermore, one reducing gas injection lance 14 may be provided for one hot blast tuyere 13, or multiple reducing gas injection lances 14 may be provided. The height positions P1 of the centers of the openings 14a of the multiple reducing gas injection lances 14 may be the same as or different from each other.

1.3 熱風羽口と還元ガス吹込ランスの開口との位置関係
 本実施形態において、還元ガス吹込ランス14の開口14aの中心の高さ位置Pは、熱風羽口13の中心の高さ位置Pと同じであるか、又は、高さ位置Pよりも下方に存在することが重要である。本発明者らの新たな知見によると、還元ガス吹込ランス14の開口14aの中心の高さ位置Pが熱風羽口13の中心の高さ位置Pよりも上方に存在する場合、還元ガス吹込ランス14から吹き込まれた還元ガスが高炉10の壁面を伝って上昇するなどして、高炉10の内部において還元ガスの偏流が生じ易い。これに対し、還元ガス吹込ランス14の開口14aの中心の高さ位置Pが熱風羽口13の中心の高さ位置Pと同じか、又は、高さ位置Pよりも下方に存在する場合、高炉10の内部において、熱風の下側に流れる還元ガスの量が増加するとともに、壁面を伝って上昇する還元ガスの量が減少し、還元ガスが高炉10の内部の径方向中心(炉中心)まで到達し易くなる。結果として、高炉10の内部における還元ガスの偏流が抑制され、還元ガスの利用効率が改善される。特に、還元ガス吹込ランス14の開口14aの中心の高さ位置Pが、熱風羽口13の中心の高さ位置Pよりも下方に存在する場合に、還元ガスの偏流を抑制する効果が一層顕著となる。
1.3 Positional Relationship Between Hot Blast Tuyere and Opening of Reducing Gas Injection Lance In this embodiment, it is important that the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is lower than the height position P2 . According to new findings by the inventors, if the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is higher than the height position P2 of the center of the hot blast tuyere 13, the reducing gas injected from the reducing gas injection lance 14 will rise along the wall surface of the blast furnace 10, and the reducing gas will likely flow unevenly inside the blast furnace 10. In contrast, when the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is lower than the height position P2 , the amount of reducing gas flowing below the hot blast inside the blast furnace 10 increases, and the amount of reducing gas rising along the wall surface decreases, making it easier for the reducing gas to reach the radial center (furnace center) inside the blast furnace 10. As a result, uneven flow of the reducing gas inside the blast furnace 10 is suppressed, and the utilization efficiency of the reducing gas is improved. In particular, when the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is lower than the height position P2 of the center of the hot blast tuyere 13, the effect of suppressing uneven flow of the reducing gas becomes more remarkable.

 図3A及びBに、還元ガス吹込ランス14の開口14aの中心の高さ位置Pが熱風羽口13の中心の高さ位置Pよりも下方に存在する場合の一例を示す。図3Aに示されるように、還元ガス吹込ランス14の開口14aの中心は、熱風羽口13の中心の真下に設けられていてもよい。すなわち、高炉10の周方向における還元ガス吹込ランス14の開口14aの中心の位置が、熱風羽口13の中心の位置と同じであってもよい。また、図3Bに示されるように、還元ガス吹込ランス14の開口14aの中心は、熱風羽口13の中心の斜め下に設けられていてもよい。すなわち、高炉10の周方向において、還元ガス吹込ランス14の開口14aの中心が、熱風羽口13の中心とは異なる位置に存在していてもよい。 3A and 3B show an example in which the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is lower than the height position P2 of the center of the hot blast tuyere 13. As shown in FIG. 3A, the center of the opening 14a of the reducing gas injection lance 14 may be located directly below the center of the hot blast tuyere 13. That is, the position of the center of the opening 14a of the reducing gas injection lance 14 in the circumferential direction of the blast furnace 10 may be the same as the position of the center of the hot blast tuyere 13. Furthermore, as shown in FIG. 3B, the center of the opening 14a of the reducing gas injection lance 14 may be located obliquely below the center of the hot blast tuyere 13. That is, the center of the opening 14a of the reducing gas injection lance 14 may be located at a position different from the center of the hot blast tuyere 13 in the circumferential direction of the blast furnace 10.

 図3Cに、還元ガス吹込ランス14の開口14aの中心の高さ位置Pが熱風羽口13の中心の高さ位置Pと同じである場合を示す。図3Cに示されるように、還元ガス吹込ランス14の開口14aは、熱風羽口13の横に設けられていてもよい。 3C shows a case where the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13. As shown in FIG. 3C, the opening 14a of the reducing gas injection lance 14 may be provided beside the hot blast tuyere 13.

1.4 熱風
 熱風羽口13から吹き込まれる熱風は、例えば、空気からなるものであってもよいし、空気を酸素富化したものであってもよい。熱風の温度は、例えば、1000℃以上である。熱風の温度は、1000℃以上2000℃以下、1000℃以上1700℃以下、1000℃以上1500℃以下、又は、1000℃以上1300℃以下であってもよい。熱風羽口13における熱風の流速(熱風の流量(m/s)/熱風羽口13の吹出口の開口面積(m))は、高炉10の操業状況に応じて、調整されてもよい。一実施形態において、熱風の流速は、後述する流速V1であってもよい。
1.4 Hot Air The hot air blown from the hot air tuyere 13 may be, for example, air or oxygen-enriched air. The temperature of the hot air is, for example, 1000°C or higher. The temperature of the hot air may be 1000°C or higher and 2000°C or lower, 1000°C or higher and 1700°C or lower, 1000°C or higher and 1500°C or lower, or 1000°C or higher and 1300°C or lower. The flow rate of the hot air in the hot air tuyere 13 (flow rate of hot air ( m3 /s)/opening area of the outlet of the hot air tuyere 13 ( m2 )) may be adjusted depending on the operating status of the blast furnace 10. In one embodiment, the flow rate of the hot air may be a flow rate V1 described later.

1.5 還元ガス
 還元ガス吹込ランス14から吹き込まれる還元ガスは、高炉10の内部において還元材として機能するガスである。すなわち、高炉10に吹き込まれる前において還元材として機能しないようなガスであっても、高炉10の内部において熱分解するなどして還元材(還元成分)を生成し得るガスであれば、本願にいう「還元ガス」に含まれるものとする。また、還元ガスの比重は、熱風羽口13から高炉10の内部へと吹き込まれる熱風の比重よりも小さい。このような還元ガスとしては、例えば、水素ガス、炭化水素ガス(例えば、メタンガス)、一酸化炭素ガス、及び、アンモニアガスから選ばれる少なくとも1種が挙げられる。特に、還元ガスが水素ガスを含む場合に、本開示の技術による一層高い効果が期待できる。還元ガス吹込ランス14から吹き込まれる還元ガスの温度は、例えば、0℃以上2000℃以下、又は、25℃以上1500℃以下であってもよい。本実施形態において、還元ガス吹込ランス14の開口14aにおける還元ガスの流速(還元ガスの流量(m/s)/還元ガス吹込ランス14の吹出口の開口面積(m))は、例えば、各還元ガスの使用温度における音速以下であってもよい。一実施形態において、還元ガス吹込ランス14から吹き込まれる還元ガスの流速は、後述する流速V2であってもよい。
1.5 Reducing Gas The reducing gas injected from the reducing gas injection lance 14 functions as a reducing agent inside the blast furnace 10. In other words, even if a gas does not function as a reducing agent before being injected into the blast furnace 10, the term "reducing gas" as used herein is included as long as it can generate a reducing agent (reducing component) inside the blast furnace 10 by thermal decomposition or the like. Furthermore, the specific gravity of the reducing gas is lower than the specific gravity of the hot air injected into the blast furnace 10 from the hot air tuyere 13. Examples of such reducing gas include at least one selected from hydrogen gas, hydrocarbon gas (e.g., methane gas), carbon monoxide gas, and ammonia gas. In particular, when the reducing gas contains hydrogen gas, the technology disclosed herein can be expected to be even more effective. The temperature of the reducing gas injected from the reducing gas injection lance 14 may be, for example, 0°C or higher and 2000°C or lower, or 25°C or higher and 1500°C or lower. In this embodiment, the flow velocity of the reducing gas at the opening 14a of the reducing gas injection lance 14 (flow rate of reducing gas ( m3 /s)/opening area of the outlet of the reducing gas injection lance 14 ( m2 )) may be, for example, equal to or less than the sonic velocity at the operating temperature of each reducing gas. In one embodiment, the flow velocity of the reducing gas injected from the reducing gas injection lance 14 may be flow velocity V2, which will be described later.

1.6 熱風の流速及び還元ガスの流速
 熱風羽口13から吹き込まれる熱風の流速V1は、特に限定されるものではないが、例えば、当該流速V1が100m/s以上1000m/s以下、中でも200m/s以上400m/s以下であると、高炉10の内部における還元ガスの偏流が一層抑制され易くなる。また、還元ガス吹込ランス14から吹き込まれる還元ガスの流速V2は、特に限定されるものではないが、例えば、当該流速V2が100m/s以上1000m/s以下、中でも200m/s以上800m/s以下であると、高炉10の内部における通気が安定し、炉内還元反応が安定的に進む操業となる。
1.6 Hot Air Flow Velocity and Reducing Gas Flow Velocity The flow velocity V1 of the hot air blown from the hot air tuyere 13 is not particularly limited, but for example, if the flow velocity V1 is 100 m/s or more and 1000 m/s or less, and particularly 200 m/s or more and 400 m/s or less, uneven flow of the reducing gas inside the blast furnace 10 is more likely to be suppressed. Furthermore, the flow velocity V2 of the reducing gas blown from the reducing gas injection lance 14 is not particularly limited, but for example, if the flow velocity V2 is 100 m/s or more and 1000 m/s or less, and particularly 200 m/s or more and 800 m/s or less, ventilation inside the blast furnace 10 is stable, resulting in operation in which the reduction reaction inside the furnace proceeds stably.

1.7 その他のガス
 還元ガス吹込ランス14からは、還元ガスとともにその他のガスが吹き込まれてもよい。その他のガスとしては、例えば、窒素ガス等の不活性ガスが挙げられる。
1.7 Other Gases Other gases may be injected together with the reducing gas from the reducing gas injection lance 14. Examples of other gases include inert gases such as nitrogen gas.

2.高炉
 本開示の技術は、高炉への還元ガス吹込方法としての側面のほか、高炉そのものとしての側面も有する。すなわち、図1に示されるように、一実施形態に係る高炉10は、
  前記高炉10のシャフト下端11axよりも下方かつ出銑口12よりも上方に設けられた熱風羽口13と、
  前記熱風羽口13の壁面内に設けられ、かつ、前記熱風羽口13の先端部13aに開口14aを有する還元ガス吹込ランス14と、を有する。
  前記還元ガス吹込ランス14から前記高炉10の内部へと吹き込まれる還元ガスは、前記高炉10の内部において還元材として機能するガスである。
  前記還元ガスの比重は、前記熱風羽口13から前記高炉10の内部へと吹き込まれる熱風の比重よりも小さい。
  前記還元ガス吹込ランス14の前記開口14aの中心の高さ位置Pは、前記熱風羽口13の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する。
2. Blast Furnace The technology of the present disclosure has an aspect as a blast furnace itself in addition to an aspect as a method for injecting reducing gas into a blast furnace. That is, as shown in FIG. 1 , a blast furnace 10 according to one embodiment includes:
A hot blast tuyere 13 provided below the shaft lower end 11ax of the blast furnace 10 and above the tap hole 12;
and a reducing gas injection lance 14 provided within the wall surface of the hot blast tuyere 13 and having an opening 14 a at the tip 13 a of the hot blast tuyere 13 .
The reducing gas injected into the inside of the blast furnace 10 from the reducing gas injection lance 14 is a gas that functions as a reducing agent inside the blast furnace 10 .
The specific gravity of the reducing gas is smaller than the specific gravity of the hot air blown into the inside of the blast furnace 10 from the hot air tuyere 13 .
The height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is located below the height position P2 .

 上述の通り、高炉10においては、前記高さ位置Pが、前記高さ位置Pよりも下方に存在する場合に、還元ガスの偏流を抑制する効果が一層高まるものと考えられる。また、還元ガスが水素ガスを含む場合に、本開示の技術による効果が一層高まるものと考えられる。 As described above, it is considered that the effect of suppressing the uneven flow of the reducing gas is further enhanced when the height position P1 is located below the height position P2 in the blast furnace 10. Furthermore, it is considered that the effect of the technology of the present disclosure is further enhanced when the reducing gas contains hydrogen gas.

3.補足
 高炉10の操業においては、例えば、高炉10の上部から高炉10の内部へと鉄鉱石(酸化鉄)やコークス等が装入される一方で、高炉10の外部の熱風炉から熱風管及び熱風羽口13を介して高炉10の内部へと熱風が吹き込まれるとともに、高炉10の外部の還元ガス供給源から還元ガス流路及び還元ガス吹込ランス14を介して高炉10の内部へと還元ガスが吹き込まれる。高炉10の内部に供給されたコークス等は、燃焼して還元ガスを発生させる。当該コークス等の燃焼によって生じた還元ガスや、還元ガス吹込ランス14から吹き込まれた還元ガスによって、酸化鉄が還元及び溶解されて、溶銑が得られる。当該溶銑は、高炉10の下部に設けられた出銑口12から出湯される。本実施形態においては、還元ガス吹込ランス14を介して高炉10の内部へと還元ガスが吹き込まれることで、その分、コークス等のカーボン含有の還元材の使用量を削減することができる。結果として、CO発生量を削減することができる。高炉10は、上記のようにして銑鉄を製造可能である限りにおいて、様々な構成を採り得る。高炉10は、例えば、上述の熱風羽口13や還元ガス吹込ランス14に加えて、その他の羽口やランスを有していてもよい。また、高炉10において、熱風羽口13よりも上方にその他の還元ガス吹込ランスが存在してもよい。熱風羽口13及び還元ガス吹込ランス14以外の高炉10の構成については、本技術分野において公知であることから、ここでは詳細な説明を省略する。
3. Supplementary Information During operation of the blast furnace 10, for example, iron ore (iron oxide), coke, etc. are charged into the blast furnace 10 from the top thereof. Meanwhile, hot air is blown into the blast furnace 10 from a hot stove outside the blast furnace 10 via a hot blast pipe and hot blast tuyere 13. Furthermore, reducing gas is blown into the blast furnace 10 from a reducing gas supply source outside the blast furnace 10 via a reducing gas flow path and a reducing gas injection lance 14. The coke, etc. supplied into the blast furnace 10 is combusted to generate reducing gas. The reducing gas generated by the combustion of the coke, etc., and the reducing gas injected from the reducing gas injection lance 14 reduce and melt the iron oxide to obtain molten iron. The molten iron is tapped from a tap hole 12 provided at the bottom of the blast furnace 10. In this embodiment, by injecting reducing gas into the blast furnace 10 through the reducing gas injection lance 14, the amount of carbon-containing reducing material used, such as coke, can be reduced accordingly. As a result, the amount of CO2 generated can be reduced. The blast furnace 10 can have various configurations as long as it is capable of producing pig iron as described above. For example, the blast furnace 10 may have other tuyere(s) and lance(s) in addition to the above-described hot blast tuyere(s) 13 and reducing gas injection lance(s) 14. Furthermore, in the blast furnace 10, other reducing gas injection lance(s) may be present above the hot blast tuyere(s) 13. The configuration of the blast furnace 10 other than the hot blast tuyere(s) 13 and reducing gas injection lance(s) 14 is known in the art, and therefore will not be described in detail here.

4.効果
 以上の通り、本実施形態によれば、還元ガス吹込ランス14が、熱風羽口13の壁面内に設けられることで、当該ランスの熱損傷等が抑制され得る。また、本実施形態によれば、還元ガス吹込ランス14の開口14aの中心の高さ位置Pが、熱風羽口13の中心の高さ位置Pと同じか、又は、高さ位置Pよりも下方に存在することで、高炉10の内部における還元ガスの偏流を抑制可能である。
4. Effects As described above, according to this embodiment, thermal damage to the reducing gas injection lance 14 can be suppressed by providing the reducing gas injection lance 14 within the wall surface of the hot blast tuyere 13. Furthermore, according to this embodiment, the height position P1 of the center of the opening 14a of the reducing gas injection lance 14 is the same as the height position P2 of the center of the hot blast tuyere 13 or is lower than the height position P2 , so that uneven flow of the reducing gas inside the blast furnace 10 can be suppressed.

 以下、実施例を示しつつ本発明についてさらに説明するが、本発明は以下の実施例に限定されるものではない。本発明は、その要旨を逸脱せず、その目的を達する限りにおいて、種々の条件を採用可能とするものである。以下の実施例においては、還元ガスとして水素ガスを採用した場合を例示するが、還元ガスの種類はこれに限定されるものではない。 The present invention will be further explained below with reference to examples, but the present invention is not limited to the following examples. The present invention allows for various conditions to be adopted as long as the object is achieved without departing from the gist of the invention. In the following examples, hydrogen gas is used as the reducing gas, but the type of reducing gas is not limited to this.

 シミュレーションモデルを使用し、還元ガスを吹き込む位置を変更しつつ、高炉内装入物の最上面での炉壁と炉中心部での水素の濃度差を比較した。具体的には、以下の先行例、実施例1~3、及び、比較例1~2の各々について、水素濃度差を求めた。 Using a simulation model, the position at which the reducing gas was injected was changed, and the difference in hydrogen concentration between the furnace wall at the top of the blast furnace load and the center of the furnace was compared. Specifically, the hydrogen concentration difference was determined for each of the following prior art examples, Examples 1-3, and Comparative Examples 1-2.

 先行例:図4の「先行例」に示されるように、ランスの先端の開口の中心が、熱風羽口の開口の中心に位置するように、熱風羽口の熱風流路内(壁面外)にランスを挿入した。熱風羽口から熱風を吹き込むとともに、ランスから水素ガスを吹き込んだ。 Prior example: As shown in the "Prior example" in Figure 4, the lance was inserted into the hot air flow path of the hot air tuyere (outside the wall surface) so that the center of the opening at the tip of the lance was positioned at the center of the opening of the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.

 実施例1:図4の「実施例1」に示されるように、ランスの先端の開口の中心が、熱風羽口の開口の中心の真下に位置するように、熱風羽口の壁面内にランスを挿入した。熱風羽口から熱風を吹き込むとともに、ランスから水素ガスを吹き込んだ。 Example 1: As shown in "Example 1" in Figure 4, a lance was inserted into the wall of the hot air tuyere so that the center of the opening at the tip of the lance was positioned directly below the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.

 実施例2:図4の「実施例2」に示されるように、ランスの先端の開口の中心が、熱風羽口の開口の中心の斜め下に位置するように、熱風羽口の壁面内にランスを挿入した。熱風羽口から熱風を吹き込むとともに、ランスから水素ガスを吹き込んだ。 Example 2: As shown in "Example 2" in Figure 4, a lance was inserted into the wall of the hot air tuyere so that the center of the opening at the tip of the lance was positioned diagonally below the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.

 実施例3:図4の「実施例3」に示されるように、ランスの先端の開口の中心の高さ位置が、熱風羽口の開口の中心の高さ位置と同じになるように、熱風羽口の壁面内にランスを挿入した。熱風羽口から熱風を吹き込むとともに、ランスから水素ガスを吹き込んだ。 Example 3: As shown in "Example 3" in Figure 4, a lance was inserted into the wall surface of the hot air tuyere so that the height position of the center of the opening at the tip of the lance was the same as the height position of the center of the opening in the hot air tuyere. Hot air was blown from the hot air tuyere, and hydrogen gas was blown from the lance.

 比較例1:図4の「比較例1」に示されるように、ランスの先端の開口の中心が、熱風羽口の開口の中心の斜め上に位置するように、熱風羽口の壁面内にランスを挿入した。熱風羽口から熱風を吹き込むとともに、ランスから水素ガスを吹き込んだ。 Comparative Example 1: As shown in "Comparative Example 1" in Figure 4, a lance was inserted into the wall of the hot air tuyere so that the center of the opening at the tip of the lance was positioned diagonally above the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.

 比較例2:図4の「比較例2」に示されるように、ランスの先端の開口の中心が、熱風羽口の開口の中心の真上に位置するように、熱風羽口の壁面内にランスを挿入した。熱風羽口から熱風を吹き込むとともに、ランスから水素ガスを吹き込んだ。 Comparative Example 2: As shown in "Comparative Example 2" in Figure 4, a lance was inserted into the wall surface of the hot air tuyere so that the center of the opening at the tip of the lance was positioned directly above the center of the opening in the hot air tuyere. Hot air was blown in from the hot air tuyere, and hydrogen gas was blown in from the lance.

 下記表1に結果を示す。 The results are shown in Table 1 below.

 表1に示される結果から明らかなように、先行例及び実施例1~3のように、還元ガス吹込ランスの開口の中心の高さ位置が熱風羽口の中心の高さ位置と同じか、それよりも下方にある場合、高炉内装入物の最上面での水素の濃度差はほぼ見られなかった。これは、羽口レベルで水素ガスと熱風とが十分に混合され、炉内で熱風とともに水素が分散されたためと考えられる。ただし、先行例のように、還元ガス吹込ランスの先端部が熱風羽口の壁面に接しておらず、熱風羽口の流路内にランス全周が露出した場合、熱風によってランスの熱損傷等が生じ易い。この点、先行例については、ランスの耐久性に関して課題がある。これに対し、実施例1~3のように、還元ガス吹込ランスを熱風羽口の壁面内に配置する(ランス全周の少なくとも一部が、熱風羽口の壁面の内側に配置される)ことで、当該課題を解決できる。すなわち、還元ガスの偏流の抑制と、ランスの熱損傷等の抑制とを両立する観点からは、先行例よりも実施例1~3のほうが有利である。 As is clear from the results shown in Table 1, when the height position of the center of the opening of the reducing gas injection lance was the same as or lower than the height position of the center of the hot blast tuyere, as in the prior art example and Examples 1 to 3, almost no difference in hydrogen concentration was observed at the top surface of the material charged into the blast furnace. This is thought to be because hydrogen gas and hot air were sufficiently mixed at the tuyere level, and hydrogen was dispersed along with the hot air within the furnace. However, as in the prior art example, when the tip of the reducing gas injection lance does not contact the wall surface of the hot blast tuyere and the entire circumference of the lance is exposed within the flow path of the hot blast tuyere, the lance is prone to thermal damage from the hot air. In this regard, the prior art example has issues with the durability of the lance. However, this issue can be resolved by arranging the reducing gas injection lance within the wall surface of the hot blast tuyere (with at least a portion of the entire circumference of the lance positioned inside the wall surface of the hot blast tuyere), as in Examples 1 to 3. In other words, from the perspective of simultaneously suppressing the uneven flow of reducing gas and suppressing thermal damage to the lance, Examples 1 to 3 are more advantageous than the prior art.

 一方、比較例1~2のように、還元ガス吹込ランスの開口の中心の高さ位置が熱風羽口の中心の高さ位置よりも上方にある場合、高炉内装入物の最上面において炉中心と炉壁部とで水素濃度に大きな差が見られた。これは、水素ガスの比重が空気(熱風)の比重よりも小さく、熱風羽口から吹き込まれる熱風に水素ガスが押されることなく、水素ガスが炉内の壁側を優先的に流れたためと考えられる。 On the other hand, when the height position of the center of the opening of the reducing gas injection lance was higher than the height position of the center of the hot blast tuyere, as in Comparative Examples 1 and 2, a large difference in hydrogen concentration was observed between the center of the furnace and the furnace wall at the top surface of the contents inside the blast furnace. This is thought to be because the specific gravity of hydrogen gas is smaller than that of air (hot blast), and the hydrogen gas was not pushed by the hot blast blown in from the hot blast tuyere, and instead flowed preferentially along the wall side of the furnace.

 以上のことから、熱風羽口の壁面内に還元ガス吹込ランスを設けることで、ランスの熱損傷等を抑制することができるといえる。また、熱風羽口の壁面内に還元ガス吹込ランスを設け、当該熱風羽口の先端部に当該ランスの開口を配置したうえで、当該ランスから還元ガスを吹き込む場合、当該ランスの開口の中心の高さ位置Pが、熱風羽口の中心の高さ位置Pと同じか、又は、高さ位置Pよりも下方に存在する場合に、高炉の内部における還元ガスの偏流を抑制することができるといえる。 From the above, it can be said that providing a reducing gas injection lance within the wall surface of a hot blast tuyere can suppress thermal damage to the lance, etc. Furthermore, when a reducing gas injection lance is provided within the wall surface of a hot blast tuyere and the opening of the lance is located at the tip of the hot blast tuyere, and reducing gas is injected from the lance, it can be said that uneven flow of reducing gas inside a blast furnace can be suppressed if the height position P1 of the center of the lance opening is the same as the height position P2 of the center of the hot blast tuyere or is lower than the height position P2 .

 以上の結果をまとめると、以下の方法(1)や高炉(2)によれば、高炉の内部へと比重の小さな還元ガスを吹き込む場合に、還元ガス吹込ランスの熱損傷等を抑制可能であり、かつ、還元ガスの偏流を抑制可能といえる。 Summarizing the above results, it can be said that when injecting a reducing gas with a low specific gravity into the interior of a blast furnace, the following method (1) and blast furnace (2) can prevent thermal damage to the reducing gas injection lance and also prevent the uneven flow of the reducing gas.

(1)高炉への還元ガス吹込方法であって、
  前記高炉のシャフト下端よりも下方かつ出銑口よりも上方に設けられた熱風羽口から、前記高炉の内部へと、熱風を吹き込むとともに、
  前記熱風羽口の壁面内に設けられ、かつ、前記熱風羽口の先端部に開口を有する還元ガス吹込ランスを介して、前記高炉の内部へと、還元ガスを吹き込むこと、を含み、
  前記還元ガスが、前記高炉の内部において還元材として機能するガスであり、
  前記還元ガスの比重が、前記熱風の比重よりも小さく、
  前記還元ガス吹込ランスの前記開口の中心の高さ位置Pが、前記熱風羽口の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する、
 高炉への還元ガス吹込方法。
(1) A method for injecting reducing gas into a blast furnace, comprising:
Hot air is blown into the blast furnace from a hot air tuyere provided below the shaft lower end of the blast furnace and above the tap hole,
Injecting a reducing gas into the blast furnace through a reducing gas injection lance that is provided within a wall surface of the hot blast tuyere and has an opening at a tip end of the hot blast tuyere,
The reducing gas is a gas that functions as a reducing agent inside the blast furnace,
The specific gravity of the reducing gas is smaller than the specific gravity of the hot air,
The height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
A method of injecting reducing gas into a blast furnace.

(2)高炉であって、
  前記高炉のシャフト下端よりも下方かつ出銑口よりも上方に設けられた熱風羽口と、
  前記熱風羽口の壁面内に設けられ、かつ、前記熱風羽口の先端部に開口を有する還元ガス吹込ランスと、
 を有し、
  前記還元ガス吹込ランスから前記高炉の内部へと吹き込まれる還元ガスが、前記高炉の内部において還元材として機能するガスであり、
  前記還元ガスの比重が、前記熱風羽口から前記高炉の内部へと吹き込まれる熱風の比重よりも小さく、
  前記還元ガス吹込ランスの前記開口の中心の高さ位置Pが、前記熱風羽口の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する、
 高炉。
(2) A blast furnace,
a hot blast tuyere provided below the shaft lower end of the blast furnace and above the tap hole;
a reducing gas injection lance provided within a wall surface of the hot air tuyere and having an opening at a tip end of the hot air tuyere;
and
the reducing gas injected from the reducing gas injection lance into the inside of the blast furnace is a gas that functions as a reducing agent inside the blast furnace,
the specific gravity of the reducing gas is lower than the specific gravity of the hot air blown into the inside of the blast furnace from the hot air tuyere,
The height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
Blast furnace.

10 高炉
 11 炉腹
 12 出銑口
 13 熱風羽口
  13a 先端部
 14 還元ガス吹込ランス
  14a 開口
10 Blast furnace 11 Furnace belly 12 Taphole 13 Hot blast tuyere 13a Tip 14 Reducing gas injection lance 14a Opening

Claims (6)

 高炉への還元ガス吹込方法であって、
  前記高炉のシャフト下端よりも下方かつ出銑口よりも上方に設けられた熱風羽口から、前記高炉の内部へと、熱風を吹き込むとともに、
  前記熱風羽口の壁面内に設けられ、かつ、前記熱風羽口の先端部に開口を有する還元ガス吹込ランスを介して、前記高炉の内部へと、還元ガスを吹き込むこと、を含み、
  前記還元ガスが、前記高炉の内部において還元材として機能するガスであり、
  前記還元ガスの比重が、前記熱風の比重よりも小さく、
  前記還元ガス吹込ランスの前記開口の中心の高さ位置Pが、前記熱風羽口の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する、
 高炉への還元ガス吹込方法。
A method for injecting reducing gas into a blast furnace, comprising:
Hot air is blown into the blast furnace from a hot air tuyere provided below the shaft lower end of the blast furnace and above the tap hole,
Injecting a reducing gas into the blast furnace through a reducing gas injection lance that is provided within a wall surface of the hot blast tuyere and has an opening at a tip end of the hot blast tuyere,
The reducing gas is a gas that functions as a reducing agent inside the blast furnace,
The specific gravity of the reducing gas is smaller than the specific gravity of the hot air,
The height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
A method of injecting reducing gas into a blast furnace.
 請求項1に記載の高炉への還元ガス吹込方法であって、
  前記高さ位置Pが、前記高さ位置Pよりも下方に存在する、
 高炉への還元ガス吹込方法。
2. The method for injecting reducing gas into a blast furnace according to claim 1,
The height position P1 is located below the height position P2 .
A method of injecting reducing gas into a blast furnace.
 請求項1又は2に記載の高炉への還元ガス吹込方法であって、
  前記還元ガスが、水素ガスを含む、
 高炉への還元ガス吹込方法。
3. The method for injecting reducing gas into a blast furnace according to claim 1 or 2,
The reducing gas comprises hydrogen gas.
A method of injecting reducing gas into a blast furnace.
 高炉であって、
  前記高炉の炉腹よりも下方かつ出銑口よりも上方に設けられた熱風羽口と、
  前記熱風羽口の壁面内に設けられ、かつ、前記熱風羽口の先端部に開口を有する還元ガス吹込ランスと、
 を有し、
  前記還元ガス吹込ランスから前記高炉の内部へと吹き込まれる還元ガスが、前記高炉の内部において還元材として機能するガスであり、
  前記還元ガスの比重が、前記熱風羽口から前記高炉の内部へと吹き込まれる熱風の比重よりも小さく、
  前記還元ガス吹込ランスの前記開口の中心の高さ位置Pが、前記熱風羽口の中心の高さ位置Pと同じであるか、又は、前記高さ位置Pよりも下方に存在する、
 高炉。
A blast furnace,
a hot blast tuyere provided below the belly of the blast furnace and above the tap hole;
a reducing gas injection lance provided within a wall surface of the hot air tuyere and having an opening at a tip end of the hot air tuyere;
and
the reducing gas injected from the reducing gas injection lance into the inside of the blast furnace is a gas that functions as a reducing agent inside the blast furnace,
the specific gravity of the reducing gas is lower than the specific gravity of the hot air blown into the inside of the blast furnace from the hot air tuyere,
The height position P1 of the center of the opening of the reducing gas injection lance is the same as the height position P2 of the center of the hot air tuyere or is located below the height position P2 .
Blast furnace.
 請求項4に記載の高炉であって、
  前記高さ位置Pが、前記高さ位置Pよりも下方に存在する、
 高炉。
5. The blast furnace according to claim 4,
The height position P1 is located below the height position P2 .
Blast furnace.
 請求項4又は5に記載の高炉であって、
  前記還元ガスが、水素ガスを含む、
 高炉。
The blast furnace according to claim 4 or 5,
The reducing gas comprises hydrogen gas.
Blast furnace.
PCT/JP2025/000349 2024-01-31 2025-01-08 Method for blowing reducing gas into blast furnace and blast furnace Pending WO2025164232A1 (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5887210A (en) * 1981-11-18 1983-05-25 Kawasaki Steel Corp Operating method for blast furnace
JPS59145710A (en) * 1983-02-09 1984-08-21 Kawasaki Steel Corp Method for adding hydrogenous raw material to tuyere part of blast furnace

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5887210A (en) * 1981-11-18 1983-05-25 Kawasaki Steel Corp Operating method for blast furnace
JPS59145710A (en) * 1983-02-09 1984-08-21 Kawasaki Steel Corp Method for adding hydrogenous raw material to tuyere part of blast furnace

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