JPWO2013172036A1 - Raw material charging method to blast furnace - Google Patents

Abstract

According to the present invention, when the raw material initially charged from the furnace top bunker charged with the raw material is O1, and subsequently the raw material charged from another furnace top bunker charged with the raw material is O2, the O2 By setting the mass to 1.1 times or less of the mass of O1, even if the amount of coke is small or a large amount of pulverized coal is injected, the air permeability in the blast furnace is ensured. In addition, it is possible to provide a raw material charging method into a blast furnace that can achieve stabilization of blast furnace operation and improvement of thermal efficiency.

Description

  The present invention relates to a raw material charging method for a blast furnace in which a raw material is charged into the furnace with a turning chute.

  In a blast furnace, generally, ore raw materials such as sintered ore, pellets and massive ore and coke are charged in layers from the top of the furnace, and combustion gas flows from the tuyere to obtain pig iron. The coke and ore raw material, which are the charged raw materials for the blast furnace, descend from the top of the furnace to the lower part of the furnace, and ore reduction and raw material temperature rise occur. The ore raw material layer is gradually deformed while filling the gaps between the ore raw materials due to the temperature rise and the load from above, and the lower part of the shaft part of the blast furnace has a very high resistance to gas and almost no gas flows. Form a layer.

Conventionally, raw material charging into a blast furnace is performed by alternately charging ore raw materials and coke, and in the furnace, ore raw material layers and coke layers are alternately layered. Further, in the lower part of the blast furnace, there are an ore raw material layer having a large ventilation resistance in which an ore called softening zone is softened and fused, and a coke slit having a relatively small ventilation resistance derived from coke.
The air permeability of this cohesive zone has a great influence on the air permeability of the entire blast furnace, and the productivity in the blast furnace is limited. When a low coke operation is performed, it is considered that the coke slit becomes extremely thin because the amount of coke used is reduced.

In order to improve the cohesive zone ventilation resistance, it is known that mixing coke into the ore raw material layer is effective, and many studies have been reported to obtain an appropriate mixing state. .
For example, in Patent Document 1, in a bell-less blast furnace, coke is charged into the ore hopper on the downstream side of the ore hopper, the coke is stacked on the ore on a conveyor, charged into the furnace top bunker, and the ore And coke are charged into the blast furnace through a turning chute.

  In Patent Document 2, ore and coke are separately stored in a bunker at the top of the furnace, and coke and ore are mixed and charged at the same time, so that a normal coke charging batch and a coke central charging batch are used. And three batches for mixing and charging are performed simultaneously.

  Furthermore, in Patent Document 3, in order to prevent the instability of the cohesive zone shape in the blast furnace operation and the decrease in the gas utilization rate near the center, and to improve the safe operation and thermal efficiency, the raw material charging method in the blast furnace is In addition, all ore and all coke are thoroughly mixed and then charged into the furnace.

JP-A-3-211210 JP 2004-107794 A Japanese Patent Publication No.59-10402

Incidentally, in order to improve the ventilation resistance of the cohesive zone, it is known that it is effective to mix coke in the ore layer as in the technique described in Patent Document 3 described above.
However, the average particle size of the typical coke described in Patent Document 3 is about 40 to 50 mm, the average particle size of the ore is about 15 mm, and the particle size of both is greatly different. If only mixed, the porosity is greatly reduced, the air permeability is deteriorated in the furnace, and there is a possibility that troubles such as gas blow-out and poor lowering of raw materials may occur.
In order to avoid these troubles, a method of forming a coke-only layer in the furnace axis can be considered. According to this method, the passage of gas through the coke layer is secured in the core portion of the furnace, so that air permeability can be improved.
However, when an operation in which a large amount of pulverized coal is blown from the tuyere is performed as a blast furnace reducing material, the air permeability is hindered by an increase in the unburned pulverized coal and the Ore / Coke ratio (the mass ratio of ore and coke). Therefore, the air permeability especially around the furnace wall is greatly deteriorated, and it cannot be said that it is sufficient to ensure the air permeability only in the core portion of the furnace. Further, when performing the low coke operation as described above, the coke layer itself in the core portion of the furnace may be insufficiently formed.

  The present invention has been developed in view of the above situation, and ensures air permeability in the blast furnace even when the amount of coke is small or when a large amount of pulverized coal is injected. An object of the present invention is to provide a raw material charging method into a blast furnace that can achieve stabilization of blast furnace operation and improvement of thermal efficiency.

That is, the gist configuration of the present invention is as follows.
1. Ore raw materials such as sintered ore, pellets, massive ore and blast furnace charging raw materials for coke are disposed at at least two furnace top bunkers arranged at the top of the blast furnace and at the outlet of the top bunker. When charging into the blast furnace using the collective hopper that mixes the raw material discharged from the furnace top bunker and supplies the swirl chute and the swirl chute,
When the raw material initially charged from the furnace top bunker charged with the raw material is O1, and then the raw material charged from another furnace top bunker charged with the raw material is O2, the mass of O2 is O1. The raw material charging method to the blast furnace which is 1.1 times or less of the mass of.

2. The raw material charging to the blast furnace according to 1 above, wherein WO2 / WO1 satisfies the range of 0.5 to 1.1, where the mass of O2 is WO2 (t) and the mass of O1 is WO1 (t). How to enter.

3. When the average angle with respect to the vertical direction of the turning chute when charging the O2 is θO2 (degrees), and the average angle with respect to the vertical direction of the turning chute when charging the O1 is θO1 (degrees), 3. The raw material charging method into the blast furnace as described in 1 or 2 above, wherein the relationship of θO1 ≦ θO2 is satisfied.

4). 4. Raw material charging to the blast furnace according to 3 above, where θO1MAX (degrees) is the maximum turning angle with respect to the vertical direction of the turning chute when charging O1, and the relationship of θO2 and θO1MAX ≦ θO2 is satisfied. How to enter.

5. When the ratio of coke mixed with O2 is O2CK (mass%) and the ratio of coke mixed with O1 is O1CK (mass%), the above 1 satisfying the relationship of O1CK ≦ O2CK The raw material charging method to the blast furnace in any one of -4.

6). 6. The raw material charging method to the blast furnace as described in 5 above, wherein the ratio of O2CK to O1CK and O2CK / O1CK satisfies a range of 1.0 to 2.0.

  According to the present invention, when the ore raw material and coke are charged into the blast furnace, two types of layers that effectively improve the air permeability are formed, so that the air permeability in the lower part of the furnace is significantly improved. The reduction rate of ore is greatly improved, even if the amount of coke is low, or even in the situation where a large amount of unburned powder derived from pulverized coal is generated in operation with high pulverized coal ratio, stable blast furnace operation should be performed. Can do.

It is a schematic diagram which shows one Embodiment of the raw material charging method to the blast furnace of this invention. (A) is a schematic diagram which shows the conventional raw material charging state according to the present invention and (b) according to the present invention. It is a schematic diagram which contrasts and shows the raw material charging state to the blast furnace by this invention, and the raw material charging state in a normal blast furnace. It is explanatory drawing which compares the raw material charging state into the blast furnace by this invention, and the raw material charging state in a normal blast furnace, and shows the reduction | restoration state, ventilation | gas_flowing / heat-transfer state, and a molten carburizing state of an upper part, a middle part, and a lower part. It is a schematic block diagram which shows the experimental apparatus which measures the high temperature property of an ore raw material.

Hereinafter, a representative embodiment of the present invention will be described with reference to the drawings.
A specific charging procedure for charging ore raw materials and coke into the blast furnace will be described with reference to FIG.
In the following description, the furnace bunker 12a contains only coke, the furnace bunker 12b contains the ore raw material and coke mixed raw material O1, and the furnace top bunker 12c contains the ore raw material and coke mixed raw material O2. , Each shall be stored.
In the figure, 10 is a blast furnace, 12a to 12c are furnace bunker, 13 is a flow rate adjusting gate, 14 is a collecting hopper, 15 is a bell-less charging device, and 16 is a turning chute. Further, θ is an angle with respect to the vertical direction of the turning chute.

As a raw material charging order from the furnace top bunker, first, the raw material charging destination of the swivel chute 16 is the furnace wall inner peripheral part of the blast furnace, and only the coke is charged from the furnace top bunker 12a charged with only coke. Thus, a central coke layer is formed in the central part of the blast furnace, and a peripheral coke layer is formed in the inner peripheral part of the furnace wall as necessary.
That is, in a state where the raw material charging destination of the turning chute 16 faces the furnace wall portion of the blast furnace, the flow rate adjusting gates 13 of the furnace top bunkers 12b and 12c are closed, and the flow rate adjusting gate 13 of only the furnace top bunker 12a is opened. By supplying only the coke stored in the furnace top bunker 12a to the turning chute 16, a central coke layer is provided at the center of the blast furnace, and a peripheral coke layer is provided at the inner peripheral portion of the furnace wall as required. Form.

Next, the mixed raw material O1 is charged from the furnace top bunker 12b, and the charging order at that time is close to the central axis of the blast furnace, that is, moves sequentially from a position where θ is small, and then the central axis of the blast furnace. It moves away from the outside, that is, moves in the direction of large θ, and finally the upper end side of the inclined side wall is inserted.
Further, the mixed raw material O2 is charged from the furnace top bunker 12c. The charging order at that time is basically the same as that of the above-mentioned O1, but in the present invention, as shown below, by providing various restrictions in the order of acquisition of the above-mentioned O1 and O2, the ventilation resistance is reduced. A low and good mixed layer can be formed.

With the above procedure as one cycle, during the operation of the blast furnace, this cycle, that is, charging of coke, charging of the mixed raw material O1, and charging of the mixed raw material O2 are repeated.
The following explanation is for the case where the mixed raw material in one cycle is the two layers of O1 and O2, but there is no problem with three or more layers, and when the adjacent layers, that is, n is a natural number, On If On + 1 satisfies the following relationship of O1 and O2, the effect of the present invention can be obtained. Further, the number of the furnace top bunker is not particularly limited, and a plurality of cuts can be performed from the same furnace top bunker.
In the present invention, the number of divisions is not particularly limited. However, if the layer structure (number of times of charging) in one cycle increases, the charging speed decreases, and therefore segregation tends to occur. Since control becomes complicated, it is preferable to set the upper limit to about 20 layers.

Here, when the ore raw material and coke are segregated in the transport equipment to the furnace top bunker, etc., only the ore raw material or coke is charged, and the other hopper bunker 12a, Although it is mixed with the coke and ore raw material charged from 12b and 12c, the ratio of the ore raw material or coke is increased and the mixed layer of the ore raw material and coke formed by the swivel chute 16 The mixing ratio becomes non-uniform.
Therefore, in the present invention, the raw material charged from the furnace top bunker 12c that subsequently charges the raw material O1 is charged to the mass (WO1) of the raw material O1 that is charged from the furnace top bunker 12b that initially charges the raw material. It is important that the mass of O2 (WO2), that is, WO2 / WO1 is 1.1 or less. That is, by making WO2 1.1 times less than WO1, the raw material O1 charged before WO2 allows the raw material O2 to be charged next to flow into the furnace center side. It prevents it. On the other hand, if WO2 exceeds 1.1 times that of WO1, the so-called dam effect inflow prevention effect using the raw material O1 for preventing inflow cannot be exhibited, and the charged raw material O1 is destroyed. As a result, the raw materials O1 and O2 due to inflowing diffuse and the ore raw material and coke are separated, resulting in nonuniform mixing.
As described above, in the present invention, the mixed raw material is divided into two parts and the charging amount is further limited to eliminate the non-uniformity of the mixing ratio. As a result, the amount of coke is small, Even when a large amount of blowing operation is performed, air permeability in the blast furnace can be secured.

Furthermore, it is necessary to prevent O2, which is a raw material to be charged later, from accumulating on the upper end side of the inclined side wall and flowing into the raw material charged into the central portion, and to eliminate unevenness at the time of charging. Therefore, WO2 / WO1 is set to a range of 0.5 to 1.1.
If WO2 / WO1 is less than 0.5, the charging range of the raw material O2 is limited. On the contrary, the non-uniformity increases at the time of charging, so WO2 / WO1 is in the range of 0.5 to 1.1. . Preferably, the raw material O1 and the raw material O2 are charged in an equal amount at a maximum of 0.5 to 1.0 to prevent the occurrence of inflow. Desirably, the charging amount of the raw material O2 is reduced by an appropriate amount from the raw material O1, and the range of 0.5 to 0.95 is prevented to prevent the occurrence of inflow.
In the present invention, it is important to satisfy the value of the WO2 / WO1, as a specific value, in the blast furnace of 5000 m ³ WO1 is 80 to 110 tons (t) of about, WO2 is 55 A range of about 110 tons (t) is desirable.

In the present invention, when θ shown in FIG. 1 (hereinafter simply referred to as θ) is θO2 when O2 is charged and θO1 when θ1 is averaged when O1 is charged, θO2 is It is preferable not to be less than θO1, that is, satisfy the relationship of θO1 ≦ θO2.
This is because θO2 is made larger than θO1, and O2, which is a raw material to be charged later, can be charged to the upper end side of the inclined side wall.
In the present invention, it is important to satisfy the above relationship, but it is preferable that θO1 be in the range of about 30 to 40 degrees and θO2 be in the range of about 35 to 45 degrees.

In the present invention, when the maximum value of θ when O1 is charged is θO1MAX, it is preferable that θO2 does not fall below θO1MAX, that is, satisfies the relationship θO1MAX ≦ θO2.
This is because θO2 is made larger than θO1, and O2, which is a raw material to be charged later, can be charged to the upper end side of the inclined side wall.
In the present invention, it is important to satisfy the above relationship, but as a specific value, θO1MAX is preferably in the range of about 35 to 40 degrees.

Further, in the present invention, when the amount of coke mixed with O2 is O2CK in mass% and the amount of coke mixed with O1 is O1CK in mass%, the relationship of O1CK ≦ O2CK is satisfied. It is preferable to do.
This is to ensure the air permeability of the entire blast furnace by improving the air permeability around the furnace wall having a large furnace volume.
In the present invention, it is important to satisfy the above relationship, but as specific values, it is preferable that O1CK is in the range of about 5 to 15% by mass and O2CK is in the range of about 10 to 20% by mass. .

In the present invention, it is more preferable that the ratio of O2CK to O1CK, that is, O2CK / O1CK satisfies the range of 1.0 to 2.0.
This is because O2CK is made larger than O1CK, and O2 as raw material is charged into the upper end side of the inclined side wall to improve the air permeability around the furnace wall with a large furnace volume. This is to ensure

  That is, in the present invention, as shown in FIG. 2, the mixed layer 12e is not formed as a single layer on the central coke layer and the peripheral coke layer 12d, but on the central coke layer and the peripheral coke layer 12d. At least two layers are formed, that is, O1 and O2 in the figure.

Then, a layer (one cycle) composed of the above-described coke layer and mixed layers O1 and O2 is sequentially formed (repeated) in the blast furnace 10 from the lower part to the upper part.
In this way, by sequentially laminating the coke layer and the layers composed of the mixed layers O1 and O2, a coke layer having a low ventilation resistance is formed from the lower part of the blast furnace to the upper part of the blast furnace. In the meantime, mixed layers O1 and O2 in which coke and ore raw materials are completely mixed are formed.

  Therefore, as shown in the right half of FIG. 3, high temperature gas mainly composed of CO flows from the tuyere blast pipe 21 provided in the hot water reservoir in the lower part of the blast furnace 10, thereby rising through the coke layer. And a gas stream rising through the mixing layer is formed. Coke is burned by the high-temperature gas flowing in from the blower pipe 21, and the ore raw material is reduced and dissolved.

Thereby, the ore raw material in the lower part of the blast furnace 10 is melted, and the coke and the ore raw material charged in the blast furnace 10 descend from the top of the furnace to the lower part of the furnace, and the reduction of the ore raw material and the ore raw material A temperature rise occurs.
For this reason, a fusion zone in which the ore material is softened is formed on the upper side of the molten layer, and the ore material is reduced on the upper side of the fusion zone.
At this time, as shown in the right half of FIG. 4, in the lower part of the blast furnace 10, the ore raw material and the coke are completely mixed in the mixed layers O1 and O2, and the coke enters between the ore raw materials. The air permeability is improved, and the high temperature gas passes directly between the ore raw materials, so there is no heat transfer delay and the heat transfer characteristics can be improved.

In addition, in the lower part of the cohesive zone of the blast furnace 10, the contact area between the ore raw material and the high-temperature gas is expanded, and carburization can be promoted. Further, in the cohesive zone, air permeability and heat transfer can be improved. Furthermore, since the ore raw material and coke are arranged close to each other in the upper part of the blast furnace 10, the coupling is a mutual activation phenomenon between the reduction reaction of the ore raw material and the gasification reaction (carbon solution loss reaction). Good reduction is performed without causing a reduction delay due to the reaction.
The reduction reaction at this time is represented by FeO + CO = Fe + CO ₂ .
The gasification reaction is represented by C + CO ₂ = 2CO.

  On the other hand, in the conventional example in which the ore and coke described above are laminated in layers, as shown in the left half of FIG. 3, ore and coke are alternately charged in the blast furnace, and the ore layer and coke are placed in the blast furnace. The layers are charged in layers. In this case, when high temperature gas mainly composed of CO is introduced from the tuyere blast pipe 21, as shown in the left half of FIG. 4, the ventilation is restricted by the reduction of the coke slit at the lower part of the cohesive zone. As the pressure loss increases, there is a problem that the contact area of the ore with the hot gas is reduced and carburization is limited.

In addition, a coke slit is formed on the upper side of the cohesive zone, and heat is conducted to the ore mainly through the coke slit, so that a heat transfer delay occurs and the heat transfer becomes insufficient, and the upper part of the blast furnace 10 Then, since the coke layer with good air permeability and the ore layer with poor air permeability are laminated, not only the rate of temperature increase is reduced, but only the reduction reaction is performed, and the above coupling reaction cannot be expected. There arises a problem that a reduction delay occurs.
However, in the present embodiment, as described above, the coke layer and the charging layer formed by the mixed layers O1 and O2 in which the coke and the ore raw material are completely mixed are laminated, so that the coke slit is formed in the mixed layer. Therefore, the gas flow is made uniform, good heat transfer is ensured and stable ventilation can be improved, and the problems of the conventional example can be solved.

  Conventionally, the amount of coke (kg) required to produce hot metal: 1 ton, that is, the coke ratio was about 350 to 365 kg / t. However, when the raw material is charged according to the present invention, the coke ratio is set to 320. It can be reduced to about ~ 335 kg / t.

In order to verify the effect of the present embodiment, using the experimental apparatus shown in FIG. 5, the change in the ventilation resistance was examined by simulating the raw material reduction and the temperature raising process in the blast furnace.
In this experimental apparatus, a furnace core tube 32 is disposed on the inner peripheral surface of a cylindrical furnace body 31, and a cylindrical heating heater 33 is disposed outside the furnace core tube 32. A graphite crucible 35 is disposed at the upper end of a cylindrical body 34 made of a refractory inside the furnace core tube 32, and a charging raw material 36 is charged into the crucible 35. A load is applied to the charged raw material 36 from above by a load loading device 38 connected via a punch bar 37 so as to be in the same level as the fused layer at the bottom of the blast furnace. A drop sampling device 39 is provided below the cylindrical body 34.

The gas adjusted by the gas mixing device 40 is sent to the crucible 35 through the lower cylindrical body 34, and the gas that has passed through the charging material 36 in the crucible 35 is analyzed by the gas analyzer 41. The heating heater 33 is provided with a thermocouple 42 for controlling the heating temperature, and the crucible 35 is controlled by controlling the heater 33 with a control device (not shown) while measuring the temperature with the thermocouple 42. Is heated to 1200-1500 ° C.
Here, as the charging raw material 36 charged in the crucible 35, the following materials were used.

Comparative Example 1 in which coke is not mixed into the ore layer at all, Comparative Example 2 in which coke is mixed in the ore layer in an amount of 34 to 84% by mass, and this mixed layer is arranged as a single layer as shown in FIG. In the ore layer, the ratio WO2 / WO1 of the mass WO1 of O1 and the mass WO2 of O2 is about 1.2, the same ratio: Invention Example 1 of about 1.1, the same ratio: about 0.9 Inventive Example 2 of the present invention, Invention Example 3 of the same ratio: about 0.5, and Invention Example 6 of the same ratio: 1.0 were respectively operated at a high pulverized coal ratio operation at a pulverized coal ratio of 148 kg / t. Further, Invention Example 4 in which the average charging angle of O1 was changed, Invention Example 5 in which the average charging angle of O2 was changed, and Invention Examples 7 and 8 in which the coke ratio in O1 was changed were carried out.
It should be noted that the output ratio (t / d) per day of the blast furnace divided by the furnace volume (m ³ ), the output ratio, the mass ratio (%) of O1, and the average charging angle (degrees) of O1 ), O1 maximum charging angle (degree), coke ratio in O1 (mass%), O2 mass ratio (%), O2 average charging angle (degree), coke ratio in O2 (mass%) These are as shown in Table 1.
In addition, the operation results in each case are shown in comparison with Table 1.

In Table 1, the coke ratio and the pulverized coal ratio are the amount of coke and the amount of pulverized coal (kg) used when producing hot metal 1t.
The reducing material ratio is the sum of the coke ratio and pulverized coal ratio.
The gas utilization rate is a ratio of the concentration of CO ₂ and CO at the top of the furnace, and is calculated by the following equation.
Gas utilization rate = CO ₂ / (CO ₂ + CO) × 100
Here, CO ₂ is the furnace top CO ₂ concentration [%]
CO is furnace top CO concentration [%]
ΔP / V is an index obtained by indexing the ventilation resistance in the blast furnace, and is calculated by the following equation.
ΔP / V = (BP−TP) / BGV
Here, BP is the blowing pressure [Pa].
TP is the furnace top pressure [Pa]
BGV is Bosch gas amount [m ³ (standard state) / min]

As shown in Table 1, since Invention Examples 1 to 8 both have a coke ratio in the range of 332 to 340 kg / t, the coke ratio is lower than that of Comparative Examples 1 to 3 in the range of 362 to 350 kg / t. It has become. However, even in this case, ΔP / V, which is an index of ventilation resistance, is suppressed to a range of 20.0 to 18.5, which is lower than the range of 22.7 to 20.8 in Comparative Examples 1 to 3. is made of. Moreover, even when the output ratio was increased to 2.5 (Invention Example 3), the ventilation resistance could be reduced with a coke ratio lower than that of Comparative Examples 1 to 3.
Further, as shown in the table, it was proved that the airflow resistance can be reduced even at a low reducing material ratio with a low coke ratio by setting the mixing ratio of coke to 14% by mass or more as described above.

  As described in the above embodiment, the present invention preferably uses reverse tilt control in which the turning chute in the blast furnace is sequentially tilted from the axial center to the outer peripheral wall side.

  Further, in the above embodiment, the case where the central coke layer and the mixed layer are formed by tilting the turning chute and opening / closing control of the flow rate adjustment gate of the furnace term bunker has been described, but the present invention is not limited thereto. A dedicated coke chute that feeds coke directly into the blast furnace shaft center is placed at a position where it does not interfere with the swivel chute, and the coke is charged directly into the blast furnace shaft core to form a central coke layer. You may make it do.

  Furthermore, although the said Example made the raw material charged from the furnace top bunker into the layer comprised by mixed layer O1 and O2, O1 and O2 also as a layer comprised by mixed layer O1, O2 and O3 As long as the relationship of O 2 and O 2 and O 3 are in accordance with the present invention, the effects of the present invention can be obtained.

DESCRIPTION OF SYMBOLS 10 Blast furnace 12a-12c Bunker 13 Flow control gate 14 Collective hopper 15 Bellless type charging device 16 Turning chute 31 Furnace body 32 Furnace core tube 33 Heating heater 34 Cylindrical body 35 Graphite crucible 36 Charging raw material 37 Punch rod 38 Load loading device 39 Dropped material sampling device 40 Gas mixing device 41 Gas analyzer 42 Thermocouple

Claims (6)

Ore raw materials such as sintered ore, pellets, massive ore and blast furnace charging raw materials for coke are disposed at at least two furnace top bunkers arranged at the top of the blast furnace and at the outlet of the top bunker. When charging into the blast furnace using the collective hopper that mixes the raw material discharged from the furnace top bunker and supplies the swirl chute and the swirl chute,
When the raw material initially charged from the furnace top bunker charged with the raw material is O1, and then the raw material charged from another furnace top bunker charged with the raw material is O2, the mass of O2 is O1. The raw material charging method to the blast furnace which is 1.1 times or less of the mass of.   The raw material for a blast furnace according to claim 1, wherein WO2 / WO1 satisfies the range of 0.5 to 1.1, where the mass of O2 is WO2 (t) and the mass of O1 is WO1 (t). The charging method.   When the average angle with respect to the vertical direction of the turning chute when charging the O2 is θO2 (degrees), and the average angle with respect to the vertical direction of the turning chute when charging the O1 is θO1 (degrees), The method of charging a raw material into a blast furnace according to claim 1 or 2, wherein a relationship of θO1 ≦ θO2 is satisfied.   The raw material for a blast furnace according to claim 3, wherein θO2 and θO1MAX ≦ θO2 are satisfied, where θO1MAX (degrees) is the maximum turning angle with respect to the vertical direction of the turning chute when the O1 is charged. The charging method.   The relation of O1CK ≦ O2CK is satisfied, where the ratio of coke mixed with O2 is O2CK (mass%) and the ratio of coke mixed with O1 is O1CK (mass%). The raw material charging method to the blast furnace in any one of 1-4.   The method of charging a raw material into a blast furnace according to claim 5, wherein the ratio of O2CK to O1CK and O2CK / O1CK satisfies a range of 1.0 to 2.0.

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