EP2796566B1 - Betriebsverfahren für einen verbrennungsofen - Google Patents

Betriebsverfahren für einen verbrennungsofen Download PDF

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Publication number
EP2796566B1
EP2796566B1 EP12860851.0A EP12860851A EP2796566B1 EP 2796566 B1 EP2796566 B1 EP 2796566B1 EP 12860851 A EP12860851 A EP 12860851A EP 2796566 B1 EP2796566 B1 EP 2796566B1
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EP
European Patent Office
Prior art keywords
pulverized coal
blast furnace
operation method
less
notches
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EP12860851.0A
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English (en)
French (fr)
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EP2796566A4 (de
EP2796566A1 (de
Inventor
Daiki Fujiwara
Akinori Murao
Shiro Watakabe
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JFE Steel Corp
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JFE Steel Corp
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Priority claimed from JP2011279954A external-priority patent/JP5923967B2/ja
Application filed by JFE Steel Corp filed Critical JFE Steel Corp
Priority to EP23184934.0A priority Critical patent/EP4283233A1/de
Priority to EP18181898.0A priority patent/EP3421618B1/de
Publication of EP2796566A1 publication Critical patent/EP2796566A1/de
Publication of EP2796566A4 publication Critical patent/EP2796566A4/de
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    • 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
    • C21B7/00—Blast furnaces
    • C21B7/16—Tuyéres
    • C21B7/163—Blowpipe assembly
    • 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
    • F27D3/00—Charging; Discharging; Manipulation of charge
    • F27D3/16—Introducing a fluid jet or current into the charge
    • 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
    • F27D3/00—Charging; Discharging; Manipulation of charge
    • F27D3/16—Introducing a fluid jet or current into the charge
    • F27D2003/168—Introducing a fluid jet or current into the charge through a lance
    • F27D2003/169—Construction of the lance, e.g. lances for injecting particles

Definitions

  • the present invention relates to a method for operating a blast furnace that includes injecting pulverized coal through a blast furnace tuyere to increase the combustion temperature, thereby improving productivity and reducing CO 2 emissions.
  • Patent Literature 1 discloses that the combustion efficiency can be improved by using pulverized coal having a volatile matter content of 25 mass% or less at a pulverized coal ratio of 150 kg/t-pig iron or more, supplying the pulverized coal and oxygen to a lance for injecting a fuel through a tuyere, and increasing the oxygen concentration in the lance to 70% by volume or more.
  • Patent Literature 1 it is also proposed in Patent Literature 1 that in the case of a single-tube lance a mixture of oxygen and pulverized coal is injected through the single-tube lance, and in the case of a double wall lance pulverized coal is injected through an inner tube of the double wall lance, and oxygen is injected through an outer tube of the double wall lance.
  • the pulverized coal ratio is the mass of pulverized coal used per ton of pig iron.
  • Patent Literature 2 discloses that a reaction between pulverized coal and oxygen is promoted by dispersing the pulverized coal utilizing asperities formed on an outer tube of a double wall lance.
  • Patent Literature 3 discloses that in a double wall lance for injecting pulverized coal through an inner tube thereof and oxygen through an outer tube thereof the contact between pulverized coal and oxygen is improved by shortening the inner tube relative to the outer tube, that is, placing a pulverized coal injecting front end of the inner tube upstream from an oxygen injecting front end of the outer tube in the injecting direction.
  • JP 2000 192119 A describing a blowing method of auxiliary fuel into a blast furnace by which the auxiliary fuel is blown into the blast furnace from an auxiliary fuel blowing tuyere. Further related art may also be found in CN 102 268 496 A .
  • a gas flowing through an outer tube of a double wall lance also functions to cool the outer tube.
  • an obstacle that interferes with the gas flow such as the asperities formed on the outer tube in Patent Literature 2
  • a heat load is applied to a slow flow region, possibly causing wear damage, such as cracking or a melting loss.
  • wear damage may induce backfire or clogging of a lance.
  • An increase in the amount of pulverized coal inevitably causes a problem of abrasion of a raised portion due to pulverized coal injected through an inner tube.
  • Patent Literature 3 Although shortening the front end of the inner tube of the double wall lance relative to the outer tube of the double wall lance as described in Patent Literature 3 may improve the contact between pulverized coal and oxygen, an oxygen flow suppresses the dispersion of pulverized coal, and the combustibility of pulverized coal is not sufficiently improved.
  • the present invention has paid attention to these problems and aims to provide a blast furnace operation method for increasing the combustion temperature and thereby reducing CO 2 emissions.
  • the present invention provides a blast furnace operation method described below.
  • the method includes injecting pulverized coal together with a carrier gas through an inner tube of the double wall lance, injecting a combustion-supporting gas through an outer tube of the double wall lance, and forming notches in a injecting front end of the inner tube of the double wall lance, wherein the concentration of oxygen in a gas composed of the carrier gas and the combustion-supporting gas in the double wall lance is 35% by volume or more.
  • the combustion temperature can be increased, and consequently CO 2 emissions can be reduced.
  • the pulverized coal ratio is 170 kg/t or more
  • the specific consumption of a combustion-supporting gas, such as oxygen can be reduced by decreasing the concentration of oxygen in the gas composed of the carrier gas and the combustion-supporting gas in the double wall lance to less than 70% by volume.
  • the notches circumferentially evenly spaced in the front end of the inner tube of the double wall lance improve the diffusion of pulverized coal and the combustion-supporting gas and further improve combustion efficiency.
  • Injecting part of oxygen for enrichment into a blast as a combustion-supporting gas through the outer tube of the double wall lance can prevent excess oxygen supply without disturbing the gas balance in the blast furnace.
  • Fig. 1 is an overall view of a blast furnace to which a blast furnace operation method according to the present embodiment is applied.
  • a tuyere 3 of a blast furnace 1 is coupled to a blow pipe 2 for blowing hot air, and a lance 4 is inserted in the blow pipe 2.
  • a combustion space called a raceway 5 is disposed over a coke layer in front of the tuyere 3 in a hot air blowing direction. Combustion and gasification of a reducing material occur mainly in this combustion space.
  • Fig. 2 illustrates the combustion state when only pulverized coal 6 is injected as a solid reducing material through the lance 4.
  • the pulverized coal 6 is injected from the lance 4 into the raceway 5 through the tuyere 3.
  • the volatile matter and fixed carbon of the pulverized coal 6 burn together with coke 7.
  • an aggregate of carbon and ash which is generally called char, is discharged from the raceway as unburned char 8.
  • the hot air velocity in front of the tuyere 3 in the hot air blowing direction is approximately 200 m/sec.
  • An oxygen zone extends approximately 0.3 to 0.5 m from a front end of the lance 4 into the raceway 5.
  • Fig. 3 illustrates the combustion mechanism in the case that only the pulverized coal (PC in the figure) 6 is injected into the blow pipe 2 through the lance 4.
  • Particles of the pulverized coal 6 injected into the raceway 5 through the tuyere 3 are heated through radiative heat transfer from flames in the raceway 5.
  • the temperature of the particles increases rapidly through radiative heat transfer and conductive heat transfer.
  • the particles start to decompose at a temperature of 300°C or more.
  • the volatile matter of the particles ignites and forms a flame.
  • the combustion temperature reaches a temperature in the range of 1400°C to 1700°C.
  • the char 8 remains. Since the char 8 is mainly composed of fixed carbon, a combustion reaction is accompanied by a carbon dissolution reaction, such as a solution-loss reaction or a hydrogen gas shift reaction.
  • Fig. 4 illustrates the combustion mechanism in the case that the pulverized coal 6, together with a combustion-supporting gas oxygen 9, is injected into the blow pipe 2 through the lance 4.
  • the pulverized coal 6 and the oxygen 9 are simply injected parallel to each other.
  • a dash-dot-dot line in the figure indicates the combustion temperature in the case that only the pulverized coal is injected as illustrated in Fig. 3 .
  • Simultaneous injecting of the pulverized coal and oxygen promotes mixing of the pulverized coal and oxygen in the vicinity of the lance and accelerates the combustion of the pulverized coal, thereby increasing the combustion temperature in the close vicinity of the lance.
  • a combustion experiment was performed with a combustion experimental apparatus illustrated in Fig. 5 .
  • Imitating the interior of a blast furnace an experiment furnace 11 is filled with coke, and the interior of a raceway 15 can be observed through an observation window.
  • a lance 14 is inserted in a blow pipe 12.
  • a hot air blown from an air-heating furnace to the blast furnace a hot air produced by a combustion burner 13 can be blasted into the experiment furnace 11 at a predetermined blast rate.
  • the oxygen enrichment level of the blast air can be controlled with the blow pipe 12.
  • One or both of pulverized coal and oxygen can be injected into the blow pipe 12 through the lance 14.
  • An exhaust gas from the experiment furnace 11 is separated into an exhaust gas and dust in a separator 16 called cyclone.
  • the exhaust gas is sent to an exhaust gas treatment system, such as an auxiliary combustion furnace.
  • the dust is collected in a collecting box 17.
  • the pulverized coal is composed of fixed carbon (FC) 71.4%, volatile matter (VM) 19.5%, and ash 9.1%.
  • the blast conditions include a blast temperature of 1200°C, a flow rate of 300 Nm 3 /hr, a blast velocity of 130 m/sec at a front end of the tuyere, and an oxygen enrichment of 6% (an oxygen concentration of 27.0%, an enrichment of 6.0% relative to an oxygen concentration of 21% in air).
  • the lance 14 was a double wall lance
  • pulverized coal was injected through an inner tube of the double wall lance
  • oxygen was injected as a combustion-supporting gas through an outer tube of the double wall lance.
  • Pulverized coal was carried by a carrier gas.
  • the carrier gas for pulverized coal was nitrogen.
  • the solid-gas ratio of pulverized coal to a carrier gas for carrying pulverized coal ranges from 10 to 25 kg/Nm 3 in the case that a powder, that is, pulverized coal is carried by a small amount of gas (high concentration transport) or 5 to 10 kg/Nm 3 in the case that pulverized coal is carried by a large amount of gas (low concentration transport).
  • the carrier gas may also be air.
  • An experiment was conducted with a focus on variations in pulverized coal flow at a pulverized coal ratio in the range of 100 to 180 kg/t.
  • oxygen was injected as a combustion-supporting gas, part of oxygen for enrichment was included in the blast so as not to change the total amount of oxygen blown into the furnace.
  • the combustion-supporting gas may also be an oxygen-enriched air.
  • the present inventors found the following in this experiment.
  • a combustion-supporting gas that is, oxygen
  • the combustion temperature is increased by increasing the oxygen concentration in an operation at a low pulverized coal ratio of less than 150 kg/t even if the pulverized coal has a volatile matter content of 25 mass% or less.
  • the combustion temperature is not increased by increasing the oxygen concentration.
  • the pulverized coal ratio is 150 kg/t or more, the combustion temperature levels off at an oxygen concentration of approximately 35% by volume.
  • Fig. 6(a) illustrates the pulverized coal flow in an operation at a low pulverized coal ratio of less than 150 kg/t. Since the lance is a straight tube having a constant diameter in the experiment, the dispersion width of pulverized coal is substantially constant. The pulverized coal flow has a substantially uniform concentration within the dispersion width at such a low pulverized coal ratio. In an operation at a high pulverized coal ratio of 150 kg/t or more, however, as illustrated in Fig. 6(b) , pulverized coal is concentrated in the center of the dispersion width.
  • pulverized coal in an operation at a high pulverized coal ratio of 170 kg/t or more, pulverized coal is highly concentrated in the center of the pulverized coal flow. Since oxygen is injected through the outer tube of the double wall lance, pulverized coal concentrated in the center of the pulverized coal flow does not come into contact with oxygen, and such unburned pulverized coal injected into the furnace interferes with aeration in the blast furnace. Even if the amount of oxygen blown is increased to promote contact with oxygen, when the amount of oxygen blown exceeds a certain threshold, as illustrated in Fig. 6(c) , the pulverized coal flow is further concentrated in the center of the surrounding oxygen flow. Thus, the contact with oxygen is not substantially promoted, and the combustion temperature levels off as described later.
  • the pulverized coal 6 and the combustion-supporting gas oxygen 9 can diffuse through the notches 23 formed in the injecting front end of the inner tube 21 of the double wall lance 4 and come into contact with each other, thereby increasing the combustion temperature.
  • pulverized coal 6 is concentrated in a central portion of a combustion-supporting gas oxygen 9. This results in poor contact between the pulverized coal 6 and the oxygen 9, and the combustion temperature levels off.
  • the notches 23 formed in the inner tube 21 of the double wall lance 4 have no wear damage trouble.
  • the combustion temperature levels off when the concentration of oxygen in a gas composed of the carrier gas for carrying pulverized coal and the combustion-supporting gas in the lance is 35% by volume or more.
  • the combustion temperature is not increased at an oxygen concentration of 35% by volume or more.
  • the combustion temperature increases even when the concentration of oxygen in a gas composed of the carrier gas and the combustion-supporting gas is 35% by volume or more. This means that the pulverized coal flow from the double wall lance 4 is not concentrated at a pulverized coal ratio of 150 kg/t or more and less than 170 kg/t.
  • the combustion temperature levels off when the concentration of oxygen in a gas composed of the carrier gas and the combustion-supporting gas in the lance is 70% by volume or more, and the combustion temperature is not increased at an oxygen concentration of more than 70% by volume.
  • the concentration of oxygen in the gas composed of the carrier gas and the combustion-supporting gas in the lance is 70% by volume or more, the combustion efficiency is not improved at a pulverized coal ratio of 170 kg/t or more, although the specific oxygen consumption increases.
  • the concentration of oxygen in the gas composed of the carrier gas and the combustion-supporting gas is 35% by volume or more and less than 70% by volume, preferably 40% by volume or more and 65% by volume or less, more preferably 45% by volume or more and 60% by volume or less, at a pulverized coal ratio of 150 kg/t or more and less than 170 kg/t or a pulverized coal ratio of 170 kg/t.
  • the upper limit of the pulverized coal ratio is 300 kg/t or less, preferably 250 kg/t or less.
  • the shape of the notches 23 in the inner tube 21 viewed in the radial direction may be tetragonal as illustrated in Fig. 11(a) , triangular as illustrated in Fig. 11(b) , or U-shaped as illustrated in Fig. 11(c) .
  • the size of the notches 23 is represented by the opening width of the notches 23 and the depth of the notches 23 from the opening to the bottom thereof.
  • the angle ⁇ made by the center of the front end and the center of the lower end of each of the notches 23, more specifically the angle ⁇ of a line segment between the center of the opening and the center of the bottom of each of the notches 23 with respect to a chord of the opening preferably ranges from 30 to 90 degrees.
  • Fig. 14 illustrates the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal as a function of the notch width.
  • the notch width was represented by the ratio of the total width of the notches to the internal circumference of the inner tube.
  • the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal were represented by ratios based on the case of the inner tube having no notch.
  • the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal increased with increasing notch width.
  • the dispersion width of the pulverized coal began to decrease at a certain notch width.
  • the ratio of the total width of the notches to the circumference of the inner tube is preferably more than 0 and 0.5 or less, more preferably 0.05 or more and 0.3 or less, still more preferably 0.1 or more and 0.2 or less.
  • Fig. 15 illustrates the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal as a function of the notch depth.
  • the notch depth was represented by the depth itself.
  • the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal was represented by ratios based on the case of the inner tube having no notch.
  • the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal increased with increasing notch depth.
  • the dispersion width of the pulverized coal began to decrease at a certain notch depth.
  • the notch depth is preferably more than 0 and 12 mm or less, more preferably 2 mm or more and 10 mm or less, still more preferably 3 mm or more and 7 mm or less.
  • Fig. 16 illustrates the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal as a function of the number of notches.
  • the number of notches was represented by the ratio of the number of the notches to the maximum number of notches.
  • the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal were represented by ratios based on the case of the inner tube having no notch.
  • the maximum number of notches is an integer part of a quotient obtained by dividing the internal circumference of the inner tube of the double wall lance by the notch width, more specifically the maximum number of notches having a predetermined width in the inner tube.
  • the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal increased with increasing number of notches.
  • the dispersion width of the pulverized coal began to decrease at a certain number of notches. This is probably because although the degree of mixing between oxygen and pulverized coal and the dispersibility of the pulverized coal increase with increasing number of notches, an excessively great number of notches results in an increased ratio of oxygen flowing through the inner tube, thereby suppressing the dispersion of pulverized coal.
  • the ratio of the number of the notches to the maximum number of notches is preferably more than 0 and 0.8 or less, more preferably 0.1 or more and 0.6 or less, still more preferably 0.2 or more and 0.5 or less.
  • Fig. 17 illustrates the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal as a function of the width of a tetragonal notch or a triangular notch.
  • the experimental results for the triangular notch is superimposed on Fig. 14 .
  • the notch width was represented by the ratio of the total width of the notches to the internal circumference of the inner tube.
  • the contact area between oxygen and pulverized coal and the dispersion width of the pulverized coal were represented by ratios based on the case of the inner tube having no notch.
  • the ratio of the total width of the notches of any shape to the circumference of the inner tube is preferably more than 0 and 0.5 or less, more preferably 0.05 or more and 0.3 or less, still more preferably 0.1 or more and 0.2 or less.
  • the lance is a stainless steel pipe, for example.
  • a lance is sometimes surrounded by a water jacket and is cooled with water, a front end of the lance cannot be surrounded by the water jacket.
  • a front end of an outer tube of a double wall lance that cannot be cooled with water is likely to change its shape with heat.
  • a pulverized coal flow may be changed and hit a tuyere, thereby causing damage to the tuyere.
  • a bent outer tube of a double wall lance may block a gap between the outer tube and an inner tube of the lance.
  • a blockage in the outer tube may result in a melting loss of the outer tube of the double wall lance or may cause damage to a blow pipe. Deformation or wear damage of a lance makes it difficult to achieve the desired combustion temperature and decrease the specific consumption of a reducing material.
  • the outer tube In order to cool an outer tube of a double wall lance, which cannot be cooled with water, the outer tube must be cooled with a gas flowing inside the outer tube. In the case that an outer tube of a double wall lance is cooled by dissipating heat into a gas flowing inside the outer tube, the flow velocity of the gas probably affects the lance temperature.
  • the present inventors measured the lance surface temperature while changing the flow velocity of a gas injected through an outer tube of a double wall lance.
  • oxygen was injected through the outer tube of the double wall lance, and pulverized coal was injected through an inner tube of the double wall lance. The flow velocity of a gas was changed with the amount of oxygen injected through the outer tube.
  • An oxygen-enriched air may be used instead of oxygen. 2% or more, preferably 10% or more, oxygen-enriched air is used. An oxygen-enriched air is used not only for cooling but also in order to improve the combustibility of pulverized coal.
  • Fig. 18 shows the measurement results.
  • the outer tube of the double wall lance was a steel pipe called 20A schedule 5S.
  • the inner tube of the double wall lance was a steel pipe called 15A schedule 90.
  • the lance surface temperature was measured while changing the total flow velocity of oxygen and nitrogen injected through the outer tube.
  • the terms "15A” and “20A” refer to the nominal outer diameter of a steel pipe according to JIS G 3459.
  • 15A denotes an outer diameter of 21.7 mm
  • 20A denotes an outer diameter of 27.2 mm.
  • the term “schedule” is the nominal thickness of a steel pipe according to JIS G 3459.
  • 20A schedule 5S denotes a thickness of 1.65 mm
  • 15A schedule 90 denotes a thickness of 3.70 mm.
  • plain steel may also be used.
  • the outer diameter of a steel pipe is specified in JIS G 3452
  • the thickness of the steel pipe is specified in JIS G 3454.
  • the lance surface temperature decreases in inverse proportion to the flow velocity of a gas injected through the outer tube of the double wall lance.
  • a double wall lance surface temperature of more than 880°C results in creep deformation and a bending of the double wall lance.
  • the outlet flow velocity in the outer tube of the double wall lance is 20 m/sec or more.
  • the double wall lance has no deformation or bending.
  • An outlet flow velocity of more than 120 m/sec in the outer tube of the double wall lance is not practical in terms of the operating cost of the equipment.
  • 120 m/sec is the upper limit of the outlet flow velocity in the outer tube of the double wall lance.
  • the outlet flow velocity may be 20 m/sec or more, if necessary.
  • Injecting part of oxygen for enrichment into a blast (as a combustion-supporting gas) through the outer tube 22 of the double wall lance 4 can prevent excess oxygen supply without disturbing the gas balance in the blast furnace and reduce the specific oxygen consumption.

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

Claims (28)

  1. Verfahren zum Betreiben eines Hochofens (1), umfassend:
    Aufbereiten von Kohlenstaub (6), der einen Gehalt an flüchtigen Bestandteilen von 25 Masse% oder weniger aufweist;
    Vorbereiten einer doppelwandigen Lanze (4), um den Kohlenstaub und ein verbrennungsunterstützendes Gas (9) durch eine Düse (3) einzublasen, wobei die doppelwandige Lanze (4) eine innere Röhre (21) und eine äußere Röhre (22) aufweist;
    Blasen von Heißluft durch die Düse;
    umfangseitiges Ausbilden einer Mehrzahl von Kerben (23) in einer Einblasstirnseite der inneren Röhre der doppelwandigen Lanze, wobei die Kerben in axialer Richtung geschnitten sind;
    Einblasen des Kohlenstaubs zusammen mit einem Trägergas durch die innere Röhre bei einem Kohlenstaubverhältnis von 150 kg/t-Roheisen oder mehr; und
    Einblasen des verbrennungsunterstützenden Gases durch die äußere Röhre der doppelwandigen Lanze,
    wobei die Sauerstoffkonzentration in einem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 35 Volumen% oder mehr ist, und dadurch gekennzeichnet, dass
    die Kerben so ausgebildet sind, dass der Kohlenstaub und das verbrennungsunterstützende Gas durch die Kerben streuen und miteinander in Kontakt kommen können.
  2. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    die Kerben in der Stirnseite der inneren Röhre der doppelwandigen Lanze über den Umfang gleichmäßig beabstandet sind.
  3. Verfahren zum Betreiben eines Hochofens nach Anspruch 2, wobei
    das Verhältnis der Gesamtbreite der Kerben zum Innenumfang der inneren Röhre der doppelwandigen Lanze mehr als 0 und 0,5 oder weniger ist.
  4. Verfahren zum Betreiben eines Hochofens nach Anspruch 3, wobei
    das Verhältnis der Gesamtbreite der Kerben zum Innenumfang der inneren Röhre der doppelwandigen Lanze 0,05 oder mehr und 0,3 oder weniger ist.
  5. Verfahren zum Betreiben eines Hochofens nach Anspruch 4, wobei
    das Verhältnis der Gesamtbreite der Kerben zum Innenumfang der inneren Röhre der doppelwandigen Lanze 0,1 oder mehr und 0,2 oder weniger ist.
  6. Verfahren zum Betreiben eines Hochofens nach Anspruch 2, wobei jede der Kerben eine Tiefe von mehr als 0 mm und 12 mm oder weniger aufweist.
  7. Verfahren zum Betreiben eines Hochofens nach Anspruch 6, wobei jede der Kerben eine Tiefe von 2 mm oder mehr und 10 mm oder weniger aufweist.
  8. Verfahren zum Betreiben eines Hochofens nach Anspruch 7, wobei jede der Kerben eine Tiefe von 3 mm oder mehr und 7 mm oder weniger aufweist.
  9. Verfahren zum Betreiben eines Hochofens nach Anspruch 2, wobei das Verhältnis der Anzahl der Kerben zu der maximalen Anzahl der Kerben mehr als 0 und 0,8 oder weniger ist, wobei die maximale Anzahl an Kerben ein ganzzahliger Teil eines durch Teilen des Innenumfangs der inneren Röhre der doppelwandigen Lanze durch die Breite einer der Kerben erhaltenen Quotienten ist.
  10. Verfahren zum Betreiben eines Hochofens nach Anspruch 9, wobei das Verhältnis der Anzahl der Kerben zu der maximalen Anzahl der Kerben 0,1 oder mehr und 0,6 oder weniger ist.
  11. Verfahren zum Betreiben eines Hochofens nach Anspruch 10, wobei
    das Verhältnis der Anzahl der Kerben zu der maximalen Anzahl der Kerben 0,2 oder mehr und 0,5 oder weniger ist.
  12. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    das verbrennungsunterstützende Gas Sauerstoff ist und ein Teil des Sauerstoffs zur Anreicherung durch die äußere Röhre der doppelwandigen Lanze in einen Wind eingeblasen wird.
  13. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    der Kohlenstaub einen Gehalt an flüchtigen Bestandteilen von 3 Masse% oder mehr und 25 Masse% oder weniger aufweist.
  14. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    das durch die äußere Röhre der doppelwandigen Lanze eingeblasene verbrennungsunterstützende Gas eine Ausströmungsgeschwindigkeit im Bereich von 20 bis 120 m/s aufweist.
  15. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    das Kohlenstaubverhältnis 170 kg/t-Roheisen oder mehr ist.
  16. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    das Kohlenstaubverhältnis 170 kg/t-Roheisen oder mehr ist und
    die Sauerstoffkonzentration in dem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 35 Volumen% oder mehr und weniger als 70 Volumen% ist.
  17. Verfahren zum Betreiben eines Hochofens nach Anspruch 16, wobei
    die Sauerstoffkonzentration in dem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 40 Volumen% oder mehr und 65 Volumen% oder weniger ist.
  18. Verfahren zum Betreiben eines Hochofens nach Anspruch 17, wobei
    die Sauerstoffkonzentration in dem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 45 Volumen% oder mehr und 60 Volumen% oder weniger ist.
  19. Verfahren zum Betreiben eines Hochofens nach Anspruch 15, wobei
    das Kohlenstaubverhältnis 170 kg/t-Roheisen oder mehr und 300 kg/t-Roheisen oder weniger ist.
  20. Verfahren zum Betreiben eines Hochofens nach Anspruch 16, wobei
    das Kohlenstaubverhältnis 170 kg/t-Roheisen oder mehr und 300 kg/t-Roheisen oder weniger ist.
  21. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    die Sauerstoffkonzentration in dem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 35 Volumen% oder mehr und weniger als 70 Volumen% ist.
  22. Verfahren zum Betreiben eines Hochofens nach Anspruch 21, wobei
    die Sauerstoffkonzentration in dem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 40 Volumen% oder mehr und 65 Volumen% oder weniger ist.
  23. Verfahren zum Betreiben eines Hochofens nach Anspruch 22, wobei
    die Sauerstoffkonzentration in dem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 45 Volumen% oder mehr und 60 Volumen% oder weniger ist.
  24. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    das Kohlenstaubverhältnis 150 kg/t-Roheisen oder mehr und 300 kg/t-Roheisen oder weniger ist.
  25. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    das Kohlenstaubverhältnis 150 kg/t-Roheisen oder mehr und weniger als 170 kg/t-Roheisen ist.
  26. Verfahren zum Betreiben eines Hochofens nach Anspruch 1, wobei
    das Kohlenstaubverhältnis 150 kg/t-Roheisen oder mehr und weniger als 170 kg/t-Roheisen ist und
    die Sauerstoffkonzentration in dem aus dem Trägergas und dem verbrennungsunterstützenden Gas zusammengesetzten Gas 35 Volumen% oder mehr und weniger als 70 Volumen% ist.
  27. Verfahren zum Betreiben eines Hochofens nach einem der Ansprüche 1 bis 26, wobei
    Kunststoffabfälle, Brennstoffe aus Müll, organische Mittel, Altholz und/oder Koks-Trockenabschreckungs-Kohlenstaub dem Kohlenstaub zugefügt wird.
  28. Verfahren zum Betreiben eines Hochofens nach Anspruch 27, wobei
    der Kohlenstaub 80 Masse% oder mehr ausmacht und Kunststoffabfälle, Brennstoffe aus Müll, organische Mittel, Altholz und/oder Koks-Trockenabschreckungs-Kohlenstaub benutzt wird.
EP12860851.0A 2011-12-21 2012-03-01 Betriebsverfahren für einen verbrennungsofen Active EP2796566B1 (de)

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JP2011279954A JP5923967B2 (ja) 2010-12-27 2011-12-21 高炉操業方法
PCT/JP2012/055893 WO2013094230A1 (ja) 2011-12-21 2012-03-01 高炉操業方法

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DE102014216336A1 (de) 2014-08-18 2016-02-18 Küttner Holding GmbH & Co. KG Verfahren zum Einblasen von Ersatzreduktionsmitteln in einen Hochofen
CN110714106B (zh) * 2019-10-30 2020-12-29 沈忠凡 一种高钛型钒钛磁铁矿的高炉优化冶炼方法
TWI758977B (zh) * 2019-11-29 2022-03-21 日商日本製鐵股份有限公司 高爐的作業方法

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EP3421618B1 (de) 2023-09-13
WO2013094230A1 (ja) 2013-06-27
CN104024440B (zh) 2016-01-20
EP2796566A4 (de) 2015-12-02
BR112014015336A2 (pt) 2017-06-13
BR112014015336A8 (pt) 2017-06-13
KR20140109964A (ko) 2014-09-16
BR112014015336B1 (pt) 2019-05-14
EP2796566A1 (de) 2014-10-29
TW201326405A (zh) 2013-07-01
TWI487791B (zh) 2015-06-11
AU2012355194A1 (en) 2014-07-24
EP3421618A1 (de) 2019-01-02
EP4283233A1 (de) 2023-11-29
CN104024440A (zh) 2014-09-03
KR101629123B1 (ko) 2016-06-09
AU2012355194B2 (en) 2015-09-03
IN2014KN01261A (de) 2015-10-16

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