JP2009221296A - Method for producing ferro coke - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing ferro coke having high cold strength as strength after carbonization and post-reaction strength after reaction with CO<SB>2</SB>gas by carbonizing a molded material consisting of an iron oxide-containing material and a carbon-containing material. <P>SOLUTION: The molded material 10, obtained by mixing the iron-containing material and the carbon-containing material and molding the mixture, is carbonized by heating for producing the ferro coke 12. In this process, a part of the iron-containing material and a part of the carbon-containing material are mixed to produce pseudo particles 6 having iron content concentration higher than that of a mixture 4 of the residue of the iron-containing material and the residue of the carbon-containing material, and the pseudo particles 6 are mixed with the mixture 4 to produce the molded material 10. Preferably, the iron content concentration of the pseudo particles 6 is higher than that of the mixture 4 by 5 mass% or more, a maximum particle diameter is 10 mm or less, and a ratio of the pseudo particles 6 in the molded material 10 is 5-50 mass%. <P>COPYRIGHT: (C)2010,JPO&amp;INPIT

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 distillation of this mixture in an ordinary 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 has been proposed in which coke after dry distillation is impregnated with an iron-containing substance to produce highly reactive coke (ferro coke) (see, for example, 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.

As described above, since ferro-coke after dry distillation contains an iron oxide-containing substance, it does not react with cold strength, that is, CO ₂ gas, compared with a formed coke not containing an ordinary iron oxide-containing substance. It can be expected that the strength in the state is lowered. 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 is a method for solving the above problems and producing ferro-coke by dry distillation of a molded product comprising an iron oxide-containing material and a carbonaceous material, and the cold strength that is the strength after dry distillation and An object of the present invention is to provide a method for producing ferro-coke capable of producing ferro-coke having high strength after reaction with CO ₂ gas.

In order to solve the above-mentioned problems, the present inventors conducted tests on ferro-coke and formed coke using a conventional general-purpose reaction test apparatus for CO ₂ gas and coke, and the ferro-coke contains iron oxide. The relationship between the rate and the cold strength and the strength after reaction with 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 the coke reacted, the reaction was stopped by switching the gas to nitrogen and cooling. 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. Comparing the time required for ferro-coke and formed coke containing no iron ore to react with 30 mass% of carbon, ferro-coke compared to formed coke containing no iron ore, the time required to reach a predetermined reaction rate. 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.

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. 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 a high iron content are added, the part derived from the pseudo particles inside the particle also contributes to the reaction, so that the effect of improving the reaction rate can be maintained and the part where the porosity increases due to the reaction can be limited. Therefore, the strength reduction of the whole ferrocoke particle | grains can be suppressed by suppressing the porosity increase of remainder. Further, if the iron content in the ferro-coke is kept constant, the iron content in the remainder other than the pseudo particles can be reduced, so that the strength before the gasification reaction, that is, in the cold state can also be improved.

The present invention has been made based on such findings, and the features thereof are as follows.
(1) When producing a ferro-coke by dry-distilling a molded product obtained by mixing an iron-containing material and a carbon-containing material and heating, a part of the iron-containing material and a part of the carbon-containing material To produce pseudo particles having an iron-containing concentration higher than the mixture of the remainder of the iron-containing substance and the remainder of the carbon-containing substance, and the pseudo particles are mixed with the mixture to form a molded product. The manufacturing method of the ferro-coke characterized by these.
(2) The method for producing ferrocoke according to (1), wherein the iron-containing concentration of the pseudo particles is 5 mass% or more higher than the iron-containing concentration of the mixture.
(3) The method for producing ferrocoke according to (1) or (2), wherein the maximum particle size of the pseudo particles is 10 mm or less.
(4) The method for producing ferro-coke according to any one of (1) to (3), wherein the ratio of the pseudo particles in the molded product is 5 to 50 mass%.

According to the present invention, the cold strength of ferro-coke and the strength after reaction with CO ₂ gas can be improved. Moreover, even when the mass ratio of the iron-containing substance in ferrocoke is increased, the decrease in cold strength and the decrease in strength after reaction with CO ₂ gas are suppressed while maintaining the effect of increasing the reaction rate. effective.

For this reason, when ferro-coke is used in a blast furnace, the generation of powder generated by the reaction with CO ₂ gas is suppressed, and an increase in pressure loss due to the use of ferro-coke is suppressed, while ferro-coke and CO ₂ gas are By increasing the reaction rate, the temperature of the heat preservation zone can be lowered, which makes it possible to reduce the ratio of reducing material in the blast furnace.

In the present invention, by mixing pseudo particles having a high iron-containing concentration in a mixture of an iron-containing material and a carbon-containing material used for the production of ferro-coke, it is derived from pseudo particles having a high iron-containing concentration in ferro-coke after dry distillation. Manufactures ferro-coke in which a portion with a high metallic iron concentration is formed. 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. By mixing the pseudo particles 6 having a high iron-containing concentration into the mixture 4 of the iron-containing material and the carbon-containing material, the portion 15 having a high metallic iron concentration derived from the pseudo particles 6 having a high iron-containing concentration in the ferrocoke after dry distillation. Can be produced. 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. Further, when compared with the case where the iron content concentration in the ferro-coke is constant, it is possible to reduce the iron content of the remainder other than the pseudo particles by mixing the pseudo particles 6 having a high iron content concentration. The cold strength before reaction can be improved as compared with the case where the pseudo particles 6 having a high particle size are not mixed.

  In the production of ferro-coke, since a mixture of an iron-containing material and a carbon-containing material used for dry distillation is formed in advance, pseudo particles having a high iron-containing concentration 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 with high iron-containing concentration is not sufficiently high compared to the parts other than the pseudo-particles, the reaction with the CO ₂ gas does not occur preferentially in the parts derived from the pseudo-particles, and the remaining reaction is also suppressed. Not very effective. 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 to the iron content 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.

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 decreases, and the increase in the porosity of the remainder cannot be suppressed. It is preferable that the substance and the carbon-containing substance be 5 mass% or more in the mixture. The addition amount of the pseudo particles is more preferably 10 mass% or more in the mixture of the iron-containing material and the carbon-containing material used for molding.

FIG. 2 is a flowchart showing an embodiment of the present invention. For example, when using carbon-containing substance 1 such as coal and iron-containing substance 2 such as iron ore as raw materials for ferro-coke for blast furnace, carbon-containing substance 1 and iron as raw materials for molding in one system (upper left side in FIG. 2) Mixed material 2 is mixed with mixer 3 to produce mixture 4, carbon-containing material 1 and iron-containing material 2 are mixed in a separate system (upper right side in FIG. 2), and molding or granulating apparatus using a molding machine To produce high iron-containing pseudo-particles 6. At this time, the high iron-containing pseudo-particles 6 increase the iron-containing concentration by increasing the iron ore blending ratio as compared with the mixture 4 produced by another system. A mixture 4 prepared by mixing both the carbon-containing substance 1 and the iron-containing substance 2 and the high iron-containing pseudo particles 6 produced by both systems are mixed by a mixer 7 to produce a mixture 8 containing pseudo particles. Is molded. In this process, a portion having a high iron content 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 high iron-containing pseudo particles 6 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 carbon-containing material 1 used in one system (upper left in FIG. 2) and the carbon-containing material 1 used in another system (upper right in FIG. 2) may be the same or of different types. May be used.

  Moreover, the same thing may be used by both systems also about the iron-containing substance 2, and a different kind of thing may be used.

In order to confirm the effect of the present invention, ferro-coke was produced by adding pseudo particles, and a reaction test between 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 was pulverized to a particle size of 3 mm or less, and iron ore was pulverized to a particle size of 1 mm or less and used for the test. As the iron ore, one containing 68.2 mass% of iron was used. A mixture of coal and iron ore was pressure-molded into a 6cc Macek mold, heat-distilled until the temperature of the molded product reached 950 ° C in a general-purpose carbonization furnace, and cooled to room temperature in a nitrogen atmosphere to produce ferro-coke. . 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 pseudo-particle addition rate was made constant at 30 mass%, and the ratio of iron ore in the mixture containing pseudo-particles containing pseudo-particles used for molding (mixed average iron ore ratio) was also made constant at 30 mass%. The relationship between the ratio of iron ore in the particles, the cold strength of ferrocoke after dry distillation, the post-reaction strength after the CO ₂ gasification test, and the reaction time was investigated. 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, but more in actual blast furnaces. Since the reaction proceeds even at a high temperature, the reaction rate was fixed at 10% by mass ratio. 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, with respect to the iron ore ratio of the portion other than the pseudo particles, ferro-coke produced by adding and forming pseudo particles having a high iron content of 5 mass% or more and dry-distilling, There was an improvement in strength after reaction. 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.

  Next, pseudo particles under the conditions that the addition rate of pseudo particles was constant at 30 mass, the ratio of iron ore in the mixture containing pseudo particles used for molding was constant at 30 mass%, and the iron content in the pseudo particles was also constant. Table 2 shows the results of studying the influence of the particle size by changing the maximum particle size of.

  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.

  Further, Table 3 shows experimental results in which the addition rate of the pseudo particles was changed under the condition that the ratio of the iron ore in the mixture containing the pseudo particles used for molding was constant at 30 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, when 5 mass% or more of pseudo particles having a high iron content are added, the reaction time is shortened and the reaction rate is increased. On the other hand, when 60 mass% of pseudo particles having a high iron content is 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 high iron content pseudo particle. (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

DESCRIPTION OF SYMBOLS 1 Carbon-containing substance 2 Iron-containing substance 3 Mixer 4 Mixture 5 Molding machine or granulating device 6 High iron containing pseudo particle 7 Mixer 8 Mixture containing pseudo particle 9 Molding machine 10 Molded article 11 Carbonization furnace 12 Ferro coke 13 Blast furnace 15 Metal Parts with high iron concentration

Claims (4)

  When producing a ferro-coke by dry distillation of a molded product obtained by mixing an iron-containing substance and a carbon-containing substance, a part of the iron-containing substance and a part of the carbon-containing substance are mixed. Producing pseudo particles having a higher iron-containing concentration than the mixture of the remainder of the iron-containing substance and the remainder of the carbon-containing substance, and mixing the pseudo particles with the mixture to form a molded product, The manufacturing method of ferro-coke.   The method for producing ferrocoke according to claim 1, wherein the iron-containing concentration of the pseudo particles is 5 mass% or more higher than the iron-containing concentration of the mixture.   The method for producing ferro-coke according to claim 1 or 2, wherein the maximum particle size of the pseudo particles is 10 mm or less.   The method for producing ferro-coke according to any one of claims 1 to 3, wherein a ratio of the pseudo particles in the molded product is 5 to 50 mass%.

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