JP2007224345A - Method for operating blast furnace - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for operating a blast furnace by which the reduction material ratio of a furnace can be reduced while preventing the permeability of the blast furnace from being deteriorated when injecting partially reduced ore from a tuyere in the blast furnace. <P>SOLUTION: In the blast furnace operation method, by which auxiliary fuel and the partially reduced iron ore are injected together with hot blast from the tuyere part in the blast furnace, the reduction rate of the iron ore is 40-80%, and the iron ore is injected to the hot blast from the downstream side than the auxiliary fuel. Alternatively, in the blast furnace operation method by which the auxiliary fuel and the partially reduced iron ore are injected from the tuyere part in the blast furnace through a lance inserted into a blowing pipe connected to the tuyere, the reducing ratio of the iron ore is 40-80%, and the lance has a double pipe structure composed of an inner pipe and an outer pipe, ther4eby injecting the iron ore and the auxiliary fuel from the outer pipe. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a blast furnace operating method for reducing a reducing material ratio.

Reducing the ratio of reducing material in the blast furnace has become an important issue in order to reduce the amount of expensive coke used, and from the viewpoint of contributing to global environmental conservation by suppressing the generation of CO ₂ from the ironmaking process.

In order to reduce the reducing material ratio of the blast furnace, improvement of reduction efficiency (shaft efficiency) and reduction of heat loss are the most basic operating factors. These two operating factors can be controlled to some extent by performing the blast furnace charge distribution control with high accuracy. By controlling the gas flow in the blast furnace near the raw material by controlling the distribution of charges, the reduction efficiency is improved by improving the utilization rate of the reducing gas (gas utilization rate η _CO = CO ₂ / (CO + CO ₂ )) By optimizing the gas flow in the vicinity of the furnace wall, heat loss from the furnace wall is reduced. However, the range in which reduction efficiency (shaft efficiency) and heat loss can be controlled is the properties of the charge used in the blast furnace (sintered ore strength, reducible RI, reduced dusting RDI, coke strength, reactivity, etc.) ). In other words, since the restrictions on air permeability are relaxed under the use of high-strength raw fuel, it is easy to reduce the reducing material ratio (coke ratio), resulting in improved reduction efficiency (shaft efficiency) and reduced heat loss. easy.

  In addition to the above, two methods for actively controlling the reduction equilibrium are known as measures for reducing the reducing material ratio.

The first method is a method for lowering the reduction equilibrium temperature. By reducing the reduction temperature, the gas composition in the FeO-Fe equilibrium is shifted to the high gas utilization rate side, and the utilization efficiency (η _CO ) of the reducing gas (CO gas) is increased, resulting in a reduction in the amount of reducing material used. It is to reduce. As a means for lowering the reduction equilibrium temperature, the use of so-called highly reactive coke is known (for example, see Non-Patent Document 1). Increase of the reducing gas utilization efficiency eta _CO by the use of highly reactive coke, and techniques to reduce the reducing agent ratio has also been disclosed (e.g., Non-Patent Document 2, Non-Patent Document 3.). In Non-Patent Document 2, when coke containing a catalyst component (Ca) that promotes reactivity is blended, both the drum test 150 rotation index DI (15, 150) and the JIS reactivity index RI representing coke reactivity are the base conditions. It is disclosed that high coke can be produced compared to As a result, Non-Patent Document 3 states that reduction of the reducing material ratio of 15 to 20 kg / t was possible.

The second method is a method of charging metallic iron into a blast furnace, and the reduction load can be reduced, so that the ratio of reducing material as a heat source can be reduced. As metallic iron, scrap, direct reduced iron (DRI, HBI, etc.), etc. are used. These iron sources are charged in a lump form from the top of the furnace, or powdered material is blown from the tuyere (for example, see Non-Patent Document 4). In addition, a method of charging reduced ore, which is not as high as metal iron, is also known. When charging reduced ore from the top and / or tuyeres of a blast furnace, it is considered appropriate to use reduced ore having a metallization rate of 40 to 80% (see, for example, Patent Document 1). ).
JP-A-8-253801 Naito Masaaki et al. "Iron and Steel" 2001, 87, p. 357-364 Nomura Seiji et al. “CAMP-ISIJ” 2003, No. 16, p. 1039 Yasuyuki Ninagawa et al. “CAMP-ISIJ” 2003, No. 16, p. 1040 K. Kunimoto et al. “JJournal of Japan Institute of Energy” 2005, 84, p. 126-133

  The above-described blowing of metallic iron from the blast furnace tuyere has many reports and is a well-known method, but the properties of metallic iron (for example, reduction rate, metalization rate, slag ratio, particle size, etc.) There are no examples of determining appropriate blowing conditions according to the conditions. Moreover, since metal iron usually refers to a metallization rate of about 90% or more, it is difficult to obtain and expensive, so the amount of metal iron used in a blast furnace has not increased.

  Therefore, by establishing a technology that appropriately uses reduced ore (hereinafter referred to as partially reduced ore), which is an iron ore with a metallization rate lower than that of metallic iron, as a raw material for blast furnace, the reduction load is reduced and the heat source is reduced. It is considered that the reduction of the reducing material ratio as a practical and important technical problem. However, since the partially reduced ore contains a large amount of FeO, when it is blown from the tuyere, FeO remains in the raceway without being reduced and is trapped in the coke layer at the back of the raceway. At the same time, the slag component is also supplied to the back of the raceway, which causes the air permeability from the raceway to the surface of the core of the furnace to deteriorate significantly. Such a problem relating to the air permeability in the furnace cannot be dealt with by the technique described in Patent Document 1.

  Therefore, the object of the present invention is to solve such a problem of the prior art and reduce the ratio of reducing material of the blast furnace while preventing the deterioration of the air permeability of the blast furnace when blowing partially reduced ore in the blast furnace. An object of the present invention is to provide a method of operating a blast furnace.

In order to achieve CO ₂ reduction and cost rationalization by reducing the reducing material ratio, it is considered that injecting auxiliary fuel such as pulverized coal, heavy oil, natural gas in the blast furnace is an essential condition. Therefore, the present inventors have repeatedly studied a method for completely proceeding the reduction of the partially reduced ore in the raceway on the premise that auxiliary fuel is used even when performing the tuyere of the partially reduced ore in the blast furnace. It was. Then, it was found that it is effective to introduce the partially reduced ore into the high-temperature combustion field formed by the ignition of the auxiliary fuel, and to rapidly raise and reduce the partially reduced ore. With the reduction rate of the ore within the specified range, the partially reduced ore and auxiliary fuel are blown from the same tuyere, and then the partially reduced ore is blown from the downstream side of the auxiliary fuel or the partially reduced ore is blown. , With a double pipe structure, partially reducing ore from the inner pipe, and auxiliary fuel such as pulverized coal, heavy oil, natural gas, etc. from the outer pipe, while the reduction of the partially reduced ore in the raceway is fully advanced, The inventors found that the deterioration of ventilation at the back of the raceway can be avoided and completed the present invention. The present invention has been made based on such findings, and the features thereof are as follows.
(1) A blast furnace operation in which auxiliary fuel and partially reduced iron ore are blown together with hot air from the tuyere of the blast furnace, and the reduction rate of the iron ore is 40% or more and 80% or less, A method for operating a blast furnace, wherein the iron ore is blown into the hot air from a downstream side of the auxiliary fuel.
(2) A blast furnace operation for blowing auxiliary fuel and partially reduced iron ore from a tuyere of a blast furnace through a lance inserted into a blow pipe connected to the tuyere, The reduction rate is 40% or more and 80% or less, the lance has a double pipe structure consisting of an inner pipe and an outer pipe, and the iron ore is blown from the inner pipe and the auxiliary fuel is blown from the outer pipe. Blast furnace operation method characterized by.
(3) The blast furnace operating method according to (2), wherein the auxiliary fuel is liquid or gas.

According to the present invention, the ratio of the reducing material can be reduced by blowing the partially reduced ore without deteriorating the air permeability of the blast furnace. Along with this, the amount of carbon input to the steelworks can be greatly reduced, and as a result, it is possible to contribute to global environmental conservation by reducing the amount of CO ₂ generated.

  First, in the blast furnace operation in which auxiliary fuel such as pulverized coal, heavy oil and natural gas is blown from the tuyere of the blast furnace and at the same time partially reduced iron ore is blown, the reduction rate of the partially reduced ore for blowing is set to 40 % Or more and 80% or less. Partially reduced ore is blown from the downstream side of the auxiliary fuel, or the lance for blowing partially reduced ore is made into a double pipe structure, partially reduced ore from the inner pipe, pulverized coal, heavy oil from the outer pipe, By injecting auxiliary fuel such as natural gas, the reduction of the partially reduced ore in the raceway is completely advanced, and the deterioration of the ventilation at the back of the raceway can be avoided. The result of the basic experiment is described.

  In the present invention, the auxiliary fuel is a fuel other than coke charged from the upper part of the blast furnace, and is usually used by blowing from the tuyere, and is a solid, liquid or gaseous fuel such as pulverized coal, heavy oil or natural gas. It is. The partially reduced ore is an ore in which a part of iron ore is reduced to a reduction rate of 40 to 80% and a metallization rate of about 30 to 75%.

  In order to clarify the effect of the reduction rate of partially reduced ore or the blowing method on the reducing property and air permeability in the raceway, a blowing experiment was conducted using a small hot model shown in FIG. The small hot model 1 has a furnace portion having a depth of 1000 mm, a width of 400 mm, and a height of 1400 mm. The coke is charged into the furnace from the upper coke charging hole 2 and the exhaust gas is discharged from the exhaust gas outflow hole 3. is there. The auxiliary fuel and the partially reduced ore were blown into the furnace through the lance 6 inserted into the blow pipe 5 into the hot air blown from the blow pipe 5 connected to the tuyere 4. 7 is the raceway, and 8 is the position where the sample was sampled after the experiment.

The reduction rate of the partially reduced ore is No. reduced to about 90% from the unreduced (reduction rate of 2.8% based on hematite Fe ₂ O ₃ ). Five types of iron ores 1 to 5 were prepared. Table 1 shows the metallic iron (M.Fe), iron oxide (FeO _x ), total iron amount (T.Fe), and reduction rate of each partially reduced ore.

The particle size of each partially reduced ore was adjusted so that the particle size of 2 mm or less would be 80 mass% (-2 mm, 80%). The blast temperature in the hot model was 1200 ° C., which was the same as that in the blast furnace, and the auxiliary fuel and the lance for partially reducing ore blowing were set as shown in Case 1 to Case 3 below. Case 1 is a case in which the partially reduced ore is blown from the upstream side of the auxiliary fuel. In FIG. 2A, the partially reduced ore is blown into the blow pipe 5 from the lance 6a and the auxiliary fuel is blown from the lance 6b. In FIG. 2, white arrows indicate the direction of hot air blowing. Case 2 is a case where partially reduced ore is blown from the downstream side of the auxiliary fuel. In FIG. 2A, auxiliary fuel is blown into the blow pipe 5 from the lance 6a, and partially reduced ore is blown from the lance 6b. Case 3 is a case in which a double pipe lance is used, and partially reduced ore is blown from the inner pipe and auxiliary fuel is simultaneously blown from the outer pipe. In FIG. 2B, partially reduced ore is blown into the blow pipe 5 from the inner pipe 6c, and auxiliary fuel is blown from the outer pipe 6d. The inner diameters of the lances 6 of Cases 1 and 2 are 12 mmφ, the inner diameter of the inner tube 6 c of Case 3 is 12 mmφ, and the slit width of the inner diameter and the outer tube is 1 mm. Each lance arrangement was used, and pulverized coal (-74 μm, 80%), heavy oil, or CH ₄ simulating LNG was used as the auxiliary fuel. The amount of partially reduced ore injected was constant at an equivalent of 50 kg / t, and the auxiliary fuel injection ratio was constant at an equivalent of 100 kg / t in all cases. The air pressure was monitored during the experiment.

  [Experiment 1] As Experiment 1, a partially reduced ore of sample No. 3 (reduction rate of about 55%) was used, pulverized coal was used as the auxiliary fuel, and the influence of the lance arrangement on the change in blowing pressure during blowing was investigated. . FIG. 3 shows the measurement results of the time variation of the blowing pressure. Blowing started at 20 minutes indicated by the arrow. According to FIG. 3, the blowing pressure gradually increased in each case of Cases 1 to 3, but reached saturation about 60 minutes after the start of blowing. It can be seen that the air blowing pressure after saturation, for example 80 minutes after the start of blowing, is clearly lower in Cases 2 and 3 than in Case 1. In order to investigate this factor, the furnace body was disassembled after the experiment was completed and visually observed, and the slag derived from the blown material was collected from the sampling position at the back of the raceway and subjected to chemical analysis. When the lance arrangement was Case 1, it was observed that a large amount of slag was held up in the back of the raceway compared to Cases 2 and 3. Table 2 shows the chemical analysis results of the slag of each case.

According to Table 2, since the FeO concentration (FeO _x ) in slag is the highest in Case 1, slag components such as FeO, SiO ₂ , and Al ₂ O ₃ are not fully reduced and the partially reduced ore is not fully reduced. It is estimated that a large amount accumulated in the back of the raceway, and as a result, the air permeability in the back of the raceway deteriorated and the air pressure was increased. The reason why the reduction rate of the partially reduced ore is increased in Cases 2 and 3 is estimated as follows. That is, in Case 2, since the partially reduced ore blowing position is downstream of the auxiliary fuel blowing position, the auxiliary fuel ignites first to form an atmosphere rich in high-temperature reducing gas (CO, H ₂ ). Since partially reduced ore is introduced into the combustion field, it is considered that the temperature is rapidly raised and reduced. Similarly, in Case 3, the temperature of the partially reduced ore is increased and reduced while being surrounded by the combustion field of the surrounding auxiliary fuel, so that it is considered that sufficient reduction proceeds. On the other hand, in the case of Case 1, since the partially reduced ore is first introduced into the hot air, it is reoxidized, the reduction rate is reduced, and the contact with the combustion flame of the auxiliary fuel is reduced. This is considered to be a factor of sex decline. It is presumed that the increase in the blowing pressure is due to the fact that as the amount of FeO supplied to the back of the raceway increases, it becomes assimilated with the slag component and easily accumulates in the low temperature part at the back of the raceway.

  [Experiment 2] Next, as Experiment 2, using the lance arrangement of Case 2 that was highly effective in Experiment 1, the influence of the initial reduction rate of the partially reduced ore on the blowing pressure and reduction rate was similarly investigated. As samples of partially reduced ores, in addition to the five types shown in Table 1, Sample No. 1 and 2, sample no. 2 and 3, sample no. 3 and 4, sample no. A mixed sample in which the reduction rate was adjusted by mixing 4 and 5 was also used. As auxiliary fuel, pulverized coal was used, and the blowing ratio was the same as in Experiment 1.

  FIG. 4 shows the relationship between the blowing pressure after 80 minutes from the start of blowing and the initial reduction rate of the partially reduced ore with almost no change in blowing pressure. According to FIG. 4, it can be seen that when the initial reduction rate exceeds about 40%, the blowing pressure rapidly decreases and reaches saturation at about 80%. FIG. 5 shows the measurement result of the reduction rate obtained from the chemical analysis of the ore sampled at the back of the raceway. As in FIG. 4, when the initial reduction rate exceeds about 40%, the reduction rate rapidly increases, and when it exceeds 60%, the reduction rate reaches approximately 95% or more. 4 and 5, the air permeability improvement effect and the reduction rate increase effect are manifested simultaneously when the initial reduction rate of the partially reduced ore is 40% or more, and both of these improvement effects tend to be saturated at 80% or more. I understand. Considering that partially reduced ores with a higher reduction rate are more expensive, it is desirable that the reduction rate be the minimum necessary from the viewpoint of producing cheap hot metal. Therefore, from the above knowledge, it is sufficient that the initial reduction rate is 40% or more and 80% or less.

  [Experiment 3] Further, as Experiment 3, in order to clarify the influence of the auxiliary fuel type, an experiment of injecting heavy oil and methane gas was performed in place of the pulverized coal of Experiment 2. Although the absolute values were slightly different, both the blast pressure change and the reduction rate showed the same change as in the case of pulverized coal. Therefore, as the auxiliary fuel, in addition to solid fuels such as pulverized coal and waste plastics, most fuels that can be injected are used, such as liquid fuels such as heavy oil, naphtha, and DME (dimethyl ether), and gas fuels such as natural gas and LPG. be able to.

  [Experiment 4] As Experiment 4, a case 3 double tube lance, which was highly effective in Experiment 1, was used. A durability test was carried out using a partially reduced ore of 3 (reduction rate 55%) and an auxiliary fuel (pulverized coal or heavy oil or methane) similar to Experiment 3. The experiment was limited to the space combustion of the blow pipe part, and a continuous combustion experiment for 20 hours was performed. After the test, the lance was removed and the appearance was checked. As a result, no change was observed when heavy oil or methane was used as the auxiliary fuel. However, when pulverized coal was used, the tip of the outer lance pipe was worn and thinned. It was. In order to suppress this, it is not economical to use an expensive wear-resistant material. Therefore, it is desirable to use a liquid fuel such as heavy oil or a gaseous fuel such as methane, which has no problem with pipe wear in the case 3 double pipe lance.

  As described above, when Experiments 1 to 4 are summarized, in the blast furnace operation in which auxiliary fuel such as pulverized coal, heavy oil, natural gas or the like is blown from the tuyere of the blast furnace and partially reduced ore is blown, reduction of partially reduced ore for injection The rate is 40% or more and 80% or less, and the partially reduced ore is blown from the downstream side of the auxiliary fuel, or the lance for blowing the partially reduced ore has a double pipe structure, the partially reduced ore from the inner pipe, heavy oil from the outer pipe, etc. It can be seen that by blowing gaseous fuel such as liquid fuel and natural gas, the reduction of the partially reduced ore in the raceway can be sufficiently advanced, and stable operation can be performed while avoiding deterioration of the airflow behind the raceway.

  FIG. 6 shows an example in which the change in the reducing material ratio of the blast furnace is calculated when the amount of pulverized coal injection is fixed at 110 kg / t and partially reduced ores with different reduction rates are injected. The case where the blowing ratio of the partially reduced ore is 0 is shown as the base condition (Base). According to FIG. 6, it can be seen that the use of the partially reduced ore having a reduction rate of 40% or more can reduce the reducing material ratio as compared with the base condition, and the effect is larger as the blowing amount is larger. For example, when partially reduced ore with a reduction rate of 60% is blown at 100 kg / t, it can be seen that the reducing material ratio can be reduced by about 8 kg / t. Along with this, the amount of carbon input to the steelworks can be greatly reduced.

  There is no particular limitation on the method for producing the partially reduced ore that satisfies the purpose of the blast furnace injection. Various methods are known for producing such partially reduced ores, such as a method of reducing iron ore pellets in a shaft furnace or a rotary hearth furnace, a method of reducing iron ore fines in a fluidized bed, For example, a method of partially reducing the packaged pellets while firing with a sintering machine. Since the method using a sintering machine is not necessarily a method aiming at a high reduction rate, as a result, the reduction rate is also about 40 to 80%, and the partially reduced ore is less expensive than the method using the shaft furnace method mentioned above. It has the advantage that it can be manufactured. Therefore, an appropriate partially reduced ore may be selected from the viewpoint of the reduction rate and price.

  The partially reduced ore produced as described above is desirably adjusted to a particle size of 2 mm or less by pulverization, sieving or the like. It is particularly desirable to adjust the particle size of particles having a particle size of 2 mm or less to 80 mass% or more (−2 mm, 80%), since powder of 2 mm or more not only becomes difficult to be pneumatically fed but also promotes pipe wear.

  The partially reduced ore is received in a dedicated tank and blown from the tuyere of the blast furnace by a known method such as air transport. The blowing amount is not particularly limited as long as the temperature of the blast furnace raceway portion is not significantly lowered. The temperature of the blast furnace raceway part (represented by the adiabatic theoretical combustion temperature, etc.) can be set appropriately by adjusting the oxygen enrichment rate, the amount of steam added, etc. according to the amount blown in the range of normal blast furnace operation.

  When a single pipe lance is used as the partially reduced ore lance, the tip position of the lance may be located downstream of the lance for blowing auxiliary fuel such as pulverized coal or LNG with respect to the flow of hot air blown into the furnace. Depending on the range in which the maximum temperature can be obtained by combustion, that is, depending on the type of auxiliary fuel, it is preferable to set the auxiliary fuel lance about 50-100 mm downstream.

As a partially reduced ore, a fine ore partially reduced in a fluidized bed was used, and a blow test in an actual blast furnace was performed. As a result of chemical analysis, the reduction rate of the partially reduced ore was 68%. The particle size was adjusted to -2 mm and about 80% by sieving. The blast furnace is a blast furnace having a bell-less charging device with an internal volume of 2828 m ³ , and standard operating conditions are a pulverized coal injection ratio of 120 kg / t and a coke ratio of 370 kg / t. In blowing the partially reduced ore, one single tube lance for blowing partially reduced ore was set at a position 100 mm downstream of the pulverized coal lance based on the above knowledge. The blowing amount was 100 kg / t. As a result, the coke ratio was 360 kg / t, which was a reduction of 10 kg / t. This value almost coincides with the theoretical value shown in FIG. Therefore, it was proved that the use of the above-mentioned partially reduced ore enables the use of expensive coke to be reduced, leading to a reduction in hot metal costs and a reduction in CO ₂ generation amount due to a reduction in heat of dry distillation.

  Partially reduced ore blowing in Example 1 was stopped and temporarily returned to standard operating conditions. As a result, the coke ratio increased to the base condition of 370 kg / t under the condition of the pulverized coal injection ratio of 120 kg / t. Next, the single pipe lance for partially reducing ore injection was removed and replaced with a double pipe lance. The installation position was 100 mm downstream of the pulverized coal lance, as in Example 1. Then, natural gas is blown from the slit between the inner pipe and outer pipe of the double pipe lance, and the blow amount is gradually increased while increasing the oxygen enrichment rate so that the theoretical combustion temperature in the raceway does not change much, The final increase was 50 kg / t. Along with this operation, the coke ratio gradually decreased to 310 kg / t. Under this condition, the same partially reduced ore as in Example 1 was blown from the inner pipe of the double pipe lance at 50 kg / t. As a result, the coke ratio was further reduced to 304 kg / t, and it was verified that the coke ratio could be reduced by about 6 kg / t by blowing partially reduced ore at 50 kg / t.

Partially reduced ore blowing blast furnace bottom of the ventilation resistance index associated with _{(K l values:. K l = (P blast} 2 -P 2) / V 1.7 However, P _blast: feed air pressure ^{(kg / cm 2), P} : feather The furnace wall static pressure (kg / cm ² ), V: Bosch gas amount (Nm ³ / t)) at 6.7 m above the mouth axis is almost unchanged from the value before blowing, and stable operation is realized. did it. From this, it is surmised that the partially reduced ore that has been blown in is sufficiently reduced without the unburned matter being held up inside the raceway and impairing the air permeability.

Schematic of a small hot model. The figure which shows arrangement | positioning of a lance. The graph which shows the time change of arrangement | positioning of a lance and a ventilation pressure. The graph which shows the relationship between a ventilation pressure and the reduction rate of a partial reduction ore. The graph which shows the relationship between the reduction rate of the ore behind a raceway, and the reduction rate of a partial reduction ore. The graph which shows the change of the reducing material ratio of a blast furnace and the reduction rate of a partial reduction ore when changing the blowing ratio of a partial reduction ore.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Small hot model 2 Coke charging hole 3 Exhaust gas outflow hole 4 Tuyere 5 Blow pipe 6 Lance 6a Lance 6b Lance 6c Inner pipe 6d Outer pipe 7 Raceway 8 Sampling position

Claims (3)

  A blast furnace operation for blowing auxiliary fuel and partially reduced iron ore together with hot air from the tuyere of the blast furnace, wherein the iron ore reduction rate is 40% or more and 80% or less, The blast furnace operating method is characterized in that the iron ore is blown from the downstream side of the auxiliary fuel.   Blast furnace operation for blowing auxiliary fuel and partially reduced iron ore from the tuyere of the blast furnace through a lance inserted into a blow pipe connected to the tuyere, wherein the reduction rate of the iron ore is 40% or more and 80% or less, wherein the lance has a double pipe structure including an inner pipe and an outer pipe, and the iron ore is blown from the inner pipe and the auxiliary fuel is blown from the outer pipe. How to operate the blast furnace.   The blast furnace operating method according to claim 2, wherein the auxiliary fuel is liquid or gas.

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