JP5386864B2 - Ferro-coke manufacturing method - Google Patents

Description

  The present invention relates to a method for producing ferrocoke, which is suitable for use as a blast furnace raw material and is produced by dry distillation using an iron-containing material and a carbon-containing material as raw materials.

The technology for producing ferro-coke by blending powdered iron ore with raw coal and producing this ferro-coke by dry-distilling this mixture in a normal chamber-type coke oven is as follows. A method of charging into a furnace, (b) a method of forming coal and iron ore cold, that is, at room temperature, and charging the molded product into a chamber-type coke oven have been studied (for example, non-patent literature). 1). However, since ordinary furnace-type coke ovens are composed of silica brick, when iron ore is charged, iron ore reacts with silica, which is the main component of silica brick, and low melting point firelite (2FeO · SiO ₂ ) is generated and causes damage to the quartz brick. For this reason, the technique which manufactures ferro-coke with a chamber-type coke oven is not implemented industrially.

  In order to avoid the above problem, a method for producing highly reactive coke by impregnating coke after dry distillation with an iron-containing substance has been proposed (for example, see Patent Document 1). In this method, it is difficult to impregnate the coke with the iron-containing substance, and it takes time to increase the iron concentration to the inside, and the productivity is greatly reduced. Moreover, the iron-containing material impregnated by the impact at the time of handling peels off, and the problem that an effect falls, etc. remains.

  In recent years, a continuous molding coke manufacturing method has been developed as a coke manufacturing method replacing the chamber furnace type coke manufacturing method. In the continuous molding coke method, a vertical shaft furnace composed of chamotte bricks instead of silica bricks is used as the carbonization furnace, and coal is molded into a predetermined size in the cold, and then charged into the shaft furnace for circulation. The coal is carbonized by heating with a heat medium gas to produce a molded coke. It has been confirmed that even if a large amount of non-slightly caking coal that is abundant in resource reserves and inexpensive is used, it is possible to produce coke that has the same strength as a normal chamber-type coke oven. When the caking property is high, the coal is softened and fused in the shaft furnace, which makes it difficult to operate the shaft furnace and causes deterioration of coke quality such as deformation and cracking.

In order to suppress fusion in the shaft furnace in the continuous coke production method, iron ore is added to the coal so as to be 15 to 40% of the total amount, and a molded product is produced coldly. A method of charging has been proposed (see, for example, Patent Document 2). In this method, since iron ore has no caking property, it is necessary to add an expensive binder to produce a molded product in a cold state. Then, the method of shape | molding the coal as a raw material and iron ore, or an iron raw material to a lump molding in the state between the heated heat | fever is proposed (for example, refer patent document 3 and patent document 4).
JP 2004-315664 A JP-A-6-65579 JP 2004-217914 A JP 2005-53982 A Fuel Association "Coke Technology Annual Report" 1958, p. 38

  However, in the said patent documents 2-4, since the thermal behavior at the time of dry distillation differs between coal and an iron ore or an iron raw material, the problem that the strength fall after dry distillation is large remains.

As described above, ferro-coke is produced by mixing a carbon-containing material such as coal and an iron oxide-containing material such as iron ore or an iron raw material as a raw material. _{Although the} gasification reaction with _two gases occurs from a relatively low temperature, the strength is significantly reduced after dry distillation. This is because ferro-coke after dry distillation contains reduced iron derived from iron oxide-containing substances, but the carbon-containing substances and reduced iron are difficult to bind together and the carbon around the reduced iron is generated by the gas generated by the reduction reaction during dry distillation. This is because the porosity of the contained material is likely to increase, so that the strength at the interface is lower than that of a normal carbon-containing material, and the strength of ferro-coke is lower than that of ordinary molded coke.

Further, assuming the inside of the blast furnace, the carbon near the iron particles is preferentially consumed by the reaction with the CO ₂ gas, so that the strength further decreases. Compared with formed coke that does not contain an iron oxide-containing substance, ferro-coke undergoes a gasification reaction with CO ₂ gas from a low temperature due to the catalytic action of iron contained therein. For this reason, at a relatively high temperature where the solution loss reaction is faster than the diffusion of CO and CO ₂ gas in the ferro-coke grains, the deteriorated layer whose porosity has increased due to the reaction compared to the formed coke containing no iron oxide-containing substance. There is a tendency for the thickness to decrease and the strength to increase after reaction. On the other hand, the solution loss reaction is slow compared to the diffusion of CO and CO ₂ gas in ferrocoke grains. At relatively low temperatures, ferrocoke tends to deteriorate into ferrocoke grains and has low strength before the reaction. Since the strength decrease is greater than that of the non-formed coke, improvement of the strength after reaction with cold and CO ₂ gas is considered an important issue.

Accordingly, the present invention solves the above problems and is a method for producing ferro-coke by dry distillation of a molded product composed of an iron-containing substance and a carbon-containing substance, wherein the cold strength, which is the strength after dry distillation, and CO 2 _An object of the present invention is to provide a method for producing ferro-coke capable of producing ferro-coke having a high strength after reaction with _two gases.

In order to solve the above-mentioned problems, the present inventors conducted tests on ferro-coke and formed coke using a conventionally used general-purpose reaction test apparatus for CO ₂ gas and coke, and the iron content of ferro-coke. The relationship between the cold strength and the post-reaction strength of CO ₂ gas was examined.

  Samples of ferro-coke and molded coke used in the test were produced using coal shrunk into two as a raw material. One of the reduced coals was used for ferro-coke after adding 30% by mass of iron ore (particle size: 1 mm or less, 100 mass%: −1 mm), and the other was used for molded coke without iron ore. Each was pressure-molded using a 6 cc Macek mold, heated to 950 ° C. in a general-purpose carbonization furnace, cooled to room temperature in a nitrogen atmosphere, and iron-ore-free formed coke and ferro-coke were produced. .

Thereafter, the coke not containing iron ore and ferro-coke were reacted with a gas mixed at a volume ratio of CO: CO ₂ = 73: 27 in a general-purpose reaction furnace set at a temperature of 970 ° C., respectively. The sample mass was measured with a balance over time, and when 30 mass% of the carbon contained in each coke reacted, the gas was switched to nitrogen to stop the reaction and cooled. Iron contained in ferrocoke was already reduced to iron after dry distillation, and no reoxidation was observed after the reaction. It was about 30 mass% reaction rate also from the mass change before and after the reaction and the analysis result of each C content. When ferrocoke and 30 mass% of carbon contained in the formed coke containing no iron ore are compared, the ferrocoke reaches a predetermined reaction rate as compared with the formed coke containing no iron ore. The reaction time is significantly reduced to 0.31 times, and the reaction rate is increased.

On the other hand, the residual rate of 9.5 mm or more after rotating 130 times at a rotation speed of 20 rotations per minute using a so-called type I drum test apparatus (cylindrical shape with an inner diameter of 130 mmΦ × 700 mm) before and after the above reaction. The strength of coke was evaluated. The particle size and sample mass before the reaction were 20 mm ± 1 mm, 100 mass% was 200 g, and after the reaction, 20 mm ± 1 mm and 100 mass% were all reacted with 200 g of the sample in a test apparatus for testing. Before the reaction, it corresponds to the cold strength of the formed coke containing no ferro-coke and iron ore, and after the reaction, it corresponds to the post-reaction strength of the formed coke containing no ferro-coke and iron ore with CO ₂ gas. In the formed coke containing no iron ore, the residual ratio of 9.5 mm or more was 93.9 mass% before the reaction, but after the reaction was 75.6 mass%, and in the ferrocoke, it was 89.8 mass% before the reaction. After the reaction, each decreased to 60.0 mass%.

By comparing the formed coke and ferro-coke, increasing the iron ore ratio can improve the reaction rate with CO ₂ gas due to the catalytic action of iron, but the cold strength decreases, especially It can be seen that the strength after reaction with the CO ₂ gas is greatly reduced.

The porosity of the cross-section of the molded coke and ferro-coke after the reaction was measured by image analysis. The porosity where the carbon is consumed by the reaction increases. In the ferrocoke after the reaction, it was found that the porosity increased from the surface to the position of about 50% from the center to the remaining surface as compared with the ferrocoke before the reaction. That is, the reaction with CO ₂ gas proceeds in a portion of 80% or more of the total volume, and the effect of the iron catalyst not only on the particle surface but also inside the particle can be expected to improve the reaction rate. On the other hand, if 30 mass% of carbon after carbonization reacts, ferro-coke has iron even before the reaction, so the ratio of carbon is relatively low, and the bond between carbons is broken by the progress of reaction with CO ₂ gas. Therefore, it is considered that the strength is greatly reduced.

  In order to investigate in more detail, when the distribution of iron, carbon and porosity was investigated by observing the cross section with an electron microanalyzer (EPMA) and an optical microscope, it was not completely mixed even in ferrocoke. It was found that in the portion where the ratio of iron is low, the porosity is low and the consumption of carbon is low, and in the portion where the ratio of iron is high, the porosity is high and the consumption of carbon is high.

  On the other hand, when paying attention to the fluidity of the carbon-containing material when forming ferro-coke, if a low-fluidity carbon-containing material is used, melting between the carbon-containing materials and between the iron-containing material and the carbon-containing material is insufficient and the strength is low. It tends to decline. Therefore, when two or more types of carbon-containing materials are used in combination, the strength is reduced due to insufficient melting between the carbon-containing materials and between the iron-containing material and the carbon-containing material in the portion where the ratio of the low-fluidity carbon-containing material is high. The carbon-containing material is sufficiently melted at the portion where the ratio of the low fluidity carbon-containing material is low, so that the strength after dry distillation can be improved.

  Therefore, from the above results, if quasi-particles with a high iron content ratio are placed in a mixture of an iron-containing material and a carbon-containing material in advance when producing ferro-coke, the reaction at a portion where the iron ratio is high will occur. Since this occurs preferentially, the portion where the porosity that causes a decrease in strength occurs is limited. Further, the carbon-containing substance in the pseudo particles has a low content of the iron-containing substance that is not derived from the pseudo particles in the ferro-coke by making the content of the low-fluidity carbon-containing substance higher than the above mixture. Since the ratio of the low-fluidity carbon-containing substance in the portion is lowered, the fluidity can be improved and the decrease in strength can be suppressed. By doing so, the strength of the part derived from the pseudo-particles may be reduced, but the ratio of the iron-containing substance is high in the part derived from the pseudo-particles, so that the strength is reduced even if the fluidity of the carbon-containing substance is increased. Since it is difficult to suppress, there is no problem since a decrease in strength due to the incorporation of a large amount of a low-flowing carbon-containing substance is not significant.

On the other hand, in the case of ferro-coke in which gasification reaction with CO ₂ gas occurs at a relatively low temperature compared to ordinary coke, CO ₂ and CO gas are relatively easily diffused to the inside, so the iron content of the ferro-coke The reaction at the high part also contributes. Therefore, if pseudo particles with high iron content and low flowable carbon-containing substance are added, the part derived from pseudo particles inside the particles also contributes to the reaction, so the porosity of the reaction is maintained while maintaining the reaction rate improvement effect. Since the increase part can be limited, the strength reduction of the whole ferro-coke particle | grains can be suppressed by suppressing the porosity increase of a remainder. Also, considering the case where the iron content in the ferro-coke and the mixing ratio of the low-flowing carbon-containing substance are constant, the remaining iron content other than the pseudo particles and the mixing ratio of the low-flowing carbon-containing substance are Since it can be reduced, the strength before the gasification reaction, that is, the cold strength can be improved.

The present invention has been made based on such findings, and the features thereof are as follows.
(1) When manufacturing a ferro-coke by dry-distilling a molded product obtained by mixing an iron-containing material and two or more types of carbon-containing materials by heating, a part of the iron-containing material and the carbon-containing material To produce pseudo particles having a higher iron-containing concentration and lower fluidity of the carbon-containing material than the mixture of the remainder of the iron-containing material and the remainder of the carbon-containing material. A method for producing ferro-coke, which comprises mixing with the mixture to form a molded product.
(2) Among the carbon-containing substances, a carbon-containing substance having a lower fluidity than a predetermined value is used as a low-fluidity carbon-containing substance, and the fluidity of the carbon-containing substance is adjusted by the content concentration of the low-fluidity carbon-containing substance. The ferromagnet according to (1), wherein the content concentration of the low-fluidity carbon-containing substance in the pseudo particles is 5 mass% or more higher than the content concentration of the low-fluidity carbon-containing substance in the mixture. Coke production method.
(3) The method for producing ferrocoke according to (1) or (2), wherein the iron-containing concentration of the pseudo particles is 5 mass% or more higher than the iron-containing concentration of the mixture.
(4) The ferro-coke production method according to any one of (1) to (3), wherein the maximum particle size of the pseudo particles is 10 mm or less.
(5) The method for producing ferro-coke according to any one of (1) to (4), wherein the ratio of the pseudo particles in the molded product is 5 to 50 mass%.

According to the present invention, when the mass ratio of the iron-containing substance and the low-flowing carbon-containing substance in the ferrocoke is made constant, the cold strength of the ferrocoke and the strength after reaction with the CO ₂ gas can be improved. it can. Further, even when the mass ratio of the iron-containing substance and the low-flowing carbon-containing substance in the ferrocoke is increased, the cold strength is reduced and the reaction with the CO ₂ gas is maintained while maintaining the effect of increasing the reaction rate. There is an effect of suppressing a decrease in the post strength.

Therefore, when the ferro coke used in the blast furnace, to suppress the flour produced from the reaction between CO ₂ gas, while suppressing an increase in pressure loss due to ferro coke used, the reaction rate of the ferro coke and CO ₂ gas By increasing the temperature, the temperature of the heat preservation zone can be lowered, thereby reducing the ratio of reducing material in the blast furnace.

In the present invention, pseudo particles having a high iron-containing concentration and a low-fluidity carbon-containing material are mixed in the mixture of the iron-containing material and the carbon-containing material used for the production of ferrocoke. Thus, ferro-coke is produced in which a portion of metal iron concentration derived from pseudo particles having a high iron-containing concentration is formed in ferro-coke after dry distillation. Fig. 1 (a) shows a schematic cross-sectional view of a ferro-coke raw material molded product before dry distillation, and Fig. 1 (b) shows a schematic cross-sectional view of ferro-coke after dry distillation. In the mixture 4 of the iron-containing substance and the carbon-containing substance, a pseudo particle having a high iron-containing concentration and a high content of the low-fluidity carbon-containing substance (hereinafter referred to as “high iron-containing and low-fluidity charcoal-containing pseudo particle”) 6) can be mixed to produce ferrocoke 12 in which a portion 15 having a high concentration of metallic iron derived from high-iron-containing and low-fluidity carbon-containing pseudoparticles 6 is formed in the ferrocoke after dry distillation. In the portion 15 where the metallic iron concentration is high, carbon can preferentially react with the CO ₂ gas due to the catalytic effect of iron, so that the reaction in the remainder other than the portion 15 where the metallic iron concentration is high is suppressed and ferro-coke. The strength reduction after the reaction of the particles can be suppressed. Moreover, when compared with the case where the iron content concentration in ferro-coke is constant, by mixing high iron-containing and low-flowing charcoal-containing pseudoparticles 6, the remaining iron content concentration (iron content) other than the pseudoparticles and low Since the content concentration (mass ratio) of the fluid carbon-containing substance can be reduced, the cold strength before the reaction can be improved as compared with the case where the high iron-containing and low-fluidity carbon-containing pseudo particles 6 are not mixed.

  The low-fluidity carbon-containing substance is a carbon-containing substance having a lower fluidity than a predetermined value among the carbon-containing substances, and the fluidity of the carbon-containing substance is determined by the Gieseler plastometer method described in JIS-M8801. Shall be evaluated. For example, when the carbon-containing substance is composed of two kinds of carbon-containing substances, the predetermined carbon dioxide-containing substance having a lower maximum fluidity (MF) measured by a Gisela plastometer is a low-fluidity carbon-containing substance. Should be set. In addition, when the carbon-containing material is composed of three or more types of carbon-containing materials, the predetermined value may be set so that the carbon-containing material having the lowest MF is usually a low-fluidity carbon-containing material. When the amount of the carbon-containing material with the lowest MF is small, the carbon-containing material with the lowest MF and the carbon-containing material with the second lowest MF are made to be low-fluidity carbon-containing materials as necessary. In addition, the average maximum fluidity (MF) of the high iron-containing and low-flowing charcoal-containing pseudoparticle portion can be lower than the average maximum fluidity (MF) of the remainder (mixture) other than the pseudoparticles. You can set a value.

  In the production of ferro-coke, a mixture of an iron-containing substance and a carbon-containing substance used for dry distillation is formed in advance, so that the high iron-containing and low-flowing carbon-containing pseudoparticles may be mixed as a raw material for molding. . Pseudo particles can be manufactured by methods such as pelletizer, compacting, briquetting, etc., but if added as a raw material for molding, the strength of the molded product can be secured, so the strength of the pseudo particles themselves can keep the shape constant. I can do it.

If the iron-containing concentration of the pseudo particles is not sufficiently high compared to the portion other than the pseudo particles, the reaction with the CO ₂ gas does not occur preferentially in the portion derived from the pseudo particles, and the remaining reaction is not very effective in suppressing the reaction. Therefore, it is desirable that the iron-containing concentration of the pseudo particles is higher by 5 mass% or more before mixing the pseudo particles, that is, compared with the iron-containing concentration of the mixture of the iron-containing material other than the pseudo particles and the carbon-containing material. . More preferably, the iron-containing concentration of the pseudo particles is 10 mass% or more higher than the balance of the mixture.

  If the mass ratio of the low-fluidity carbon-containing substance in the pseudo particles is not sufficiently high compared to the portion other than the pseudo particles, the effect of improving the fluidity does not appear and the effect of improving the strength is not so much. Therefore, it is desirable that the mass ratio of the low-fluidity carbon-containing substance in the pseudo particles is 5 mass% or more higher than the mass ratio of the low-fluidity carbon-containing substance in the mixture. The fluidity of the carbon-containing substance is evaluated by the Gisela plastometer method described in JIS-M8801, as described above. In particular, the mass ratio of the iron-containing substance and the low-fluidity carbon-containing substance in ferrocoke is determined. In the case where the fluidity of the low-fluidity carbon-containing substance is 5 ddpm or less, the fluidity improvement effect in the portion other than the pseudo particles is high, and the effect obtained by the method of the present invention is large. There are cases where organic binders such as pitch are used in the granulation and molding of pseudo particles, but the temperature range where these binders melt is compared to the temperature range where coal melts (although it varies depending on the coal, approximately 350 ° C to 500 ° C) Since it is low, it is desirable to exclude it when evaluating the fluidity of the carbon-containing substance of the pseudo particle.

In the ferro-coke after dry distillation, the porosity increases due to the preferential reaction with CO ₂ in the blast furnace at a portion where the concentration of pseudo iron-derived metallic iron is high. On the other hand, the increase in the porosity of the remaining portion can be suppressed, but the portion with a high porosity becomes a structural defect that causes a decrease in the strength of the ferrocoke particles. Since ferro-coke is a brittle material, even if the amount of defects is the same, it is affected by the size of the defects, so that the maximum particle size of the pseudo particles is preferably 10 mm or less. In addition, if there are too many parts that are preferentially deteriorated in ferro-coke, the residual porosity control effect cannot be expected, and the strength of ferro-coke particles may not be maintained after the reaction, so the amount of pseudo particles added is It is preferable to be 50 mass% or less in the mixture of the iron-containing material and the carbon-containing material used for molding. On the other hand, when the amount of pseudo particles added is too small, the amount of preferential reaction with CO ₂ gas is reduced, and the increase in the porosity of the remainder cannot be suppressed. The total amount of all the iron-containing materials and carbon-containing materials to be used is preferably 5 mass% or more (the ratio of pseudo particles in the molded product is 5 mass% or more). The addition amount of the pseudo particles is more preferably 10 mass% or more (the ratio of the pseudo particles in the molded product is 10 mass% or more) of the total amount of all iron-containing materials and carbon-containing materials used for molding.

FIG. 2 is a flowchart showing an embodiment of the present invention. For example, when the carbon-containing material 1 such as coal and the iron-containing material 2 such as iron ore are used as raw materials for ferro-coke for blast furnace, the fluidity of the carbon-containing material 1b is lower than the fluidity of the carbon-containing material 1a. In addition, the blending ratio of the carbon-containing material is adjusted so that the ratio of the low-fluidity coal in the carbon-containing material 1b is higher than that of the carbon-containing material 1a. Carbon-containing material 1a and iron-containing material 2a are mixed by mixing machine 3 as a raw material for molding in one system (upper left in Fig. 2) to produce mixture 4, and carbon is contained in another system (upper right in Fig. 2). The substance 1b and the iron-containing substance 2b are mixed and granulated using a molding machine or a granulating apparatus to produce high iron-containing and low-flowing charcoal-containing pseudo particles 6. At this time, the high iron content and low fluidity coal-containing pseudo-particles 6 increase the iron ore blending ratio as compared with the mixture 4 produced by other systems so that the iron content concentration becomes high, and the low fluidity carbon content Mix many substances to lower the fluidity of carbon-containing substances. The mixture 4 produced by both systems, in which the carbon-containing material 1a and the iron-containing material 2a are mixed, and the high iron-containing and low-flowing charcoal-containing pseudoparticles 6 are mixed by a mixer 7 to produce a mixture 8 containing pseudoparticles. Then, the molding 10 is molded by the molding machine 9. In this process, a portion containing a large amount of carbon-containing material having a high iron content and low fluidity is formed in the molded product 10. This molded product 10 is carbonized in a carbonization furnace 11 and cooled to produce ferrocoke 12. During the carbonization process, carbon-containing substances such as coal lose volatile components and partly melt and resolidify into coke, and iron ore is partly reduced to iron. In the ferro-coke 12, which is a product after dry distillation, a portion having a high iron content derived from the pseudo iron particles 6 containing high iron content and low fluidity charcoal is formed. If this ferro-coke 12 is used in the blast furnace 13, the portion having a high iron content reacts preferentially, so that the reaction rate is improved, the remaining reaction is suppressed, and the strength decreases after the reaction with the CO ₂ gas. Can be suppressed. Therefore, generation | occurrence | production of the powder in a blast furnace can be suppressed, and since a heat preservation zone temperature can be lowered | hung by improvement of reaction rate, reduction of a reducing material ratio is attained.

  Note that the iron-containing material 2a used in one system (upper left in FIG. 2) and the iron-containing material 2b used in another system (upper right in FIG. 2) may be the same or of different types. May be used.

In order to confirm the effect of the present invention, ferro-coke was produced by adding pseudo particles to a mixture of coal and iron ore, and a reaction test of ferro-coke and CO ₂ gas was performed under the following conditions.

Ferro-coke was produced by dry distillation of coal and iron ore. Coal and iron ore were pulverized to a particle size of 1 mm or less and used for testing. As the iron ore, one containing 68.2 mass% of iron was used. Coal has a maximum flow rate (MF) of 2 ddpm and an average maximum reflectivity of 1.7% as measured with a Gieseler plastometer, and an average maximum reflectivity of 1.0% with a maximum flow rate (MF) of 156 ddpm. % Of slime coal. These two types of coal were mixed and used, but non-coking coal having a relatively low maximum fluidity (MF) value was used as the low-flowing carbon-containing substance. A mixture of coal and iron ore with pseudo particles is pressure-molded into a 6cc Macek mold, heated and distilled in a general-purpose dry distillation furnace until the temperature of the molded product reaches 950 ° C, and cooled to room temperature in a nitrogen atmosphere. Coke was produced. At the time of molding, 5 mass% of a polyvinyl alcohol aqueous solution was added as a binder in order to ensure the strength after molding. The same binder was added during the granulation of the pseudo particles, but the amount of binder added to the molded product after molding was made constant. Thereafter, ferro-coke produced with various compositions was reacted with a gas mixed at a ratio of CO: CO ₂ = 73: 27 in a general-purpose reactor set at a temperature of 970 ° C. The sample mass was measured over time with a balance, and when the predetermined mass of carbon contained in the coke reacted, the gas was switched to nitrogen to stop the reaction and cooled. Iron contained in the ferrocoke has already been reduced to iron after dry distillation, and reoxidation was not observed even after the reaction under the test conditions. From the analysis results of the mass change before and after the reaction and the respective C content, the reaction rate was almost predetermined. The strength of coke was evaluated by the residual rate of 9.5 mm or more after 130 rotations at a rotation speed of 20 rotations per minute using a so-called type I drum test apparatus (inner diameter 130 mmΦ × 700 mm cylinder) before and after the reaction. did. In addition, as for the particle size and sample mass before reaction, 20 g ± 1 mm was subjected to a test with 200 g of the sample, and after the reaction, 20 g ± 1 mm was reacted with a 200 g sample.

First, the rate of addition of pseudo particles is constant at 30 mass%, and the ratio of iron ore in the mixture containing pseudo particles containing pseudo particles used for molding (the average iron ore ratio of the molded product) is constant at 30 mass%. The ratio of the iron ore and low-flowing coal in the pseudo particles, the cold strength of ferro-coke after dry distillation, CO ₂ was examined a relationship between strength after reaction of the gas after trials and the reaction time. The reaction rate of coke and CO ₂ gasification in the blast furnace is said to be about 20-30%, and this test is an evaluation that specializes in reactions at low temperatures, and higher temperatures in actual blast furnaces. However, since the reaction proceeds, the reaction rate was fixed at 10 mass% of carbon in ferrocoke. Further, the pseudo particles used in this test were produced by granulating with a pelletizer, and those having a particle size of 3 to 5 mm were used. The experimental results are shown in Table 1. As a comparative example, the results of ferro-coke produced by simply mixing, molding and dry distillation of iron ore and coal without adding pseudo particles are also shown.

  According to Table 1, ferro-coke produced by adding and shaping pseudo particles having a high iron ore ratio of 5 mass% or more with respect to the iron ore ratio (iron ore ratio in the mixture) other than the pseudo particles. Then, compared with the comparative example, the cold strength and the strength after reaction were improved. Moreover, it was found that the reaction time required for 10 mass% of the contained carbon to react was shortened, and the reaction rate was increased.

  Also, molding is performed by adding 5 mass% or more pseudo particles having a high ratio of low-flowing carbon content to the low-flowing carbon-containing material ratio of the portion other than the pseudo particles (ratio of low-flowing carbon-containing material in the mixture). Even in the ferrocoke produced by dry distillation, the cold strength and post-reaction strength were improved as compared with the comparative example.

  Next, the maximum particle size of the pseudo particles is changed under the condition that the addition rate of the pseudo particles is constant at 30 mass%, the iron ore ratio in the pseudo particles and the mass ratio of the low-flowing carbon-containing substance are also constant. Table 2 shows the results of studying the effects of the above.

  According to Table 2, even if the particle size of the pseudo particles is changed, there is no significant difference in the cold strength, but when the maximum particle size is 15 mm, the strength after the reaction is slightly reduced. I understand that. This is probably because the part derived from pseudo particles in the ferro-coke preferentially reacted, and as a result, the part with high porosity was coarsened, resulting in a decrease in strength after reaction.

  Furthermore, Table 3 shows the experimental results in which the addition rate of the pseudo particles was changed under the condition that the ratio of the molded product average iron ore was constant at 30 mass%, and the ratio of the molded product average low-fluidity carbon-containing material was also fixed at 10 mass%. The pseudo particles were produced by granulating with a pelletizer, and those having a particle size of 3 to 5 mm were used.

  According to Table 3, compared with the comparative example which does not add a pseudo particle, when pseudo particles are added 5 mass% or more, it turns out that reaction time is shortened and the reaction rate is quick. On the other hand, when 60 mass% of pseudo particles are added, the cold strength and post-reaction strength tend to be lower than when pseudo particles are not added. This is probably because the high part of the iron ore occupies most of the ferro-coke particles, and the effect of suppressing the remaining reaction is reduced.

  As described above, in the ferrocoke produced by the method of the present invention, it was confirmed that the cold strength and the post-reaction strength at 970 ° C. which is a relatively low temperature were improved, and the reaction rate was increased. .

The image figure of the molding and ferro-coke which added the pseudo iron containing high iron content and low fluidity charcoal. (A) Ferro-coke raw material molding before carbonization, (b) Ferro-coke after carbonization The flowchart which shows one Embodiment of this invention.

Explanation of symbols

1 (1a, 1b) Carbon-containing material 2 (2a, 2b) Iron-containing material 3 Mixer 4 Mixture 5 Molding machine or granulating device 6 High iron-containing and low-flowing charcoal-containing pseudoparticles 7 Mixer 8 Mixture with pseudoparticles 9 Molding Machine 10 Molded Product 11 Carbonization Furnace 12 Ferro Coke 13 Blast Furnace 15 Metal Iron Concentration High

Claims (1)

When producing a ferro-coke by dry-distilling a molded product formed by mixing iron ore and two or more kinds of coals having different mean maximum fluidity (MF) and heating.
Mixing a portion of the iron ore and a portion of the coal , the iron content concentration is 5 mass% or more higher than the iron content concentration of the mixture of the remainder of the iron ore and the remainder of the coal , and the maximum particle size is Pseudoparticles of 10 mm or less, wherein coal having a lower MF than a predetermined value is set as low-fluidity coal, the fluidity of the coal is adjusted by the content concentration of the low-fluidity coal, The content concentration of the low-flowing coal is 5 mass% or more higher than the content concentration of the low-flowing coal in the mixture to produce pseudo particles having a coal flowability lower than that of the mixture. ,
A method for producing ferro-coke, wherein the pseudo particles are mixed with the mixture to form a molded product having a ratio of the pseudo particles of 5 to 50 mass% .

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