KR101246523B1 - Method of producing ferro-coke - Google Patents

Abstract

When manufacturing a ferrocoke by carbonizing a molded product composed of an iron oxide-containing material and a carbonaceous-containing material, it is possible to prevent cracks and thermal cracks generated during the drying of the molded product, to increase the circular yield at the exit of the drying furnace, and to produce the ferrocoke in the furnace. It is providing a manufacturing method of ferro coke which is hard to be broken even when it is charged to and can reduce a yield. Specifically, when the molded product formed by mixing the iron oxide-containing material and the carbonaceous-containing material is carbonized by heating to produce ferrocoke, the heating rate in the temperature range of the surface temperature of the molded product is 550 to 650 ° C. The method for producing ferrocoke is used, which is dried at 20 ° C / min or less.

Description

Manufacturing method of ferro coke {METHOD OF PRODUCING FERRO-COKE}

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing ferroc coke, which is produced by carbonization of coal and iron ore which are suitable for use as a blast furnace feed.

As a technique for mixing ferrous iron ore with raw coal and distilling the mixture in a conventional chamber oven to produce ferrocoke, 1) a powder mixture of coal and iron ore is converted into 2) a method of charging coal and iron ore at cold or room temperature, and charging the molded product into a silo type coke oven (eg, The Fuel Society of Japan). Technical Yearbook '' 1958, p. 38). However, since the conventional silo coke is composed of silica brick, iron ore reacts with silica, which is the main component of silica brick, when iron ore is charged. 2FeOSiO ₂ ) is produced, which causes damage to the silica brick. For this reason, the technique of manufacturing ferro coke in a silo type coke oven is not implemented industrially.

In recent years, as a coke manufacturing method which is replaced with the silo coke manufacturing method, the continuous molding coke manufacturing method is developed. In the continuous shaping coke process, a vertical shaft brick furnace composed of chamotte bricks rather than silica bricks is used as a carbonization oven, and coal is formed into a predetermined size by cold work. After that, the coal is charged into the shaft furnace, and carbonized into coal by heating using a circulating gas for heat carrier to produce molded coke. Although abundant resource reserves and a large amount of cheap non-slightly caking coal are used, it has been confirmed that coke having strength equivalent to that of a conventional silo coke furnace can be produced, but the cohesiveness of the coal used If the caking property is high, the coal briquettes soften and fusion in the shaft furnace, making it difficult to operate the shaft and at the same time causing deterioration of coke quality such as deformation and cracking.

In order to suppress fusion in the shaft furnace in the continuous coke production method, a method of adding iron ore to coal at an amount of 15 to 40% of the total amount, producing a molded product by cold, and charging the shaft furnace has been proposed ( See, for example, Japanese Patent Application Laid-open No. Hei 6-65579). In this method, iron ore is not caking-free, and therefore, it is necessary to add an expensive binder to prepare a molded product in a cold state. Therefore, a method of forming coal and iron ore or iron raw material as a raw material into a lump molded product in a heated hot state is also proposed (for example, Japanese Patent Laid-Open No. 2004-217914, 2005-53982). Reference). However, in Japanese Patent Laid-Open Publication Nos. Hei 6-65579 and No. 2005-53982, since the thermal behavior at the time of dry distillation is different in coal and iron ore or iron raw materials, Problems of deterioration of the coke quality, such as deformation and cracking of the moldings, remain.

On the other hand, in the manufacture of molded coke using only coal as the main raw material, in order to suppress the deterioration of the coke quality such as deformation and cracking during drying of the molded product made of the molded coke, the heating pattern when drying the molded product is examined. A method of designing an optimal heating rate according to the temperature of the molding is proposed (see, for example, Japanese Patent Application Laid-Open No. 52-23103 and No. 7-102660).

As described above, in the production of ferro coke in which coal and iron ore or iron raw materials are used as raw materials, problems such as deformation and cracking of molded products during dry distillation have not been solved. Ferrocoke is a mixture of coal (hereinafter referred to as carbon-containing material) and iron ore or iron raw material (hereinafter referred to as iron oxide-containing material), It is expected that the thermal and mechanical properties in the fabric are significantly different from those in the manufacture of the molded coke, and the deformation and the cracking behavior of the molded product in the drying process are expected to be different.

The present invention solves the above problems, and when the ferro coke is manufactured by carbonizing a molded product comprising an iron oxide-containing material and a carbonaceous-containing material, cracks and thermal cracks generated during drying of the molded product are eliminated. It is an object of the present invention to provide a method for producing ferrocoke, which can be prevented, to increase the circular yield at the exit side of the dry distillation furnace, and not to be broken even when the ferrocoke is charged into the blast furnace.

Features of the present invention for solving such a problem are as follows.

In order to solve the above technical problem, the present invention provides a method for producing ferrocoke by carbonizing a molded article obtained by mixing iron oxide-containing material and carbonaceous-containing material by heating, wherein the surface temperature of the molded article is 550 to 650 ° C. Provided is a method for producing ferrocoke, characterized in that the heating rate in the phosphorus temperature range is 5 ° C / min or more and 20 ° C / min or less.

According to the present invention, when the molded article mixed with the iron oxide-containing material and the carbonaceous-containing material is carbonized, the generation of thermal stress in the inside of the molded product is suppressed, and the yield decrease when producing ferrocoke is prevented. At the same time, it is possible to prevent cracking before blast furnace charging and in the blast furnace.

Incidentally, the heating rate in the present invention is not the average heating temperature (ΔT / t) obtained by dividing the elevated temperature ΔT ° C by the time t required for the elevated temperature, but the instantaneous heating rate (temperature gradient of the heat pattern (dT / dt) Say).

1 is a graph showing the relationship between the surface temperature and the maximum thermal stress of coal moldings.
2 is a graph showing the relationship between the surface temperature and the maximum thermal stress of the 90% coal and 10% iron ore molding.
3 is a graph showing the heating rate dependence of the surface temperature and the maximum thermal stress of the coal molding.
4 is a graph showing the heating rate dependence of the surface temperature and the maximum thermal stress of the 90% coal and 10% iron ore moldings.
5 is a graph showing the relationship between temperature and line shrinkage of 100% coal and a mixture of coal and iron ore.

The present inventors have studied the method for producing ferrocoke, performed thermal and mechanical property values of moldings in which iron oxide-containing materials and carbonaceous-containing materials, which are raw materials of ferrocoke, were measured, and thermal stress analysis based on these values ( thermal stress analysis and at the same time, based on the results of analysis of deformation or breakage of the molded part under heat treatment under various conditions, the crack control of the molded product mixed with the iron oxide-containing material and carbonaceous-containing material The present invention has been completed by finding an optimal heating method. In the present invention, the iron oxide-containing material is reduced iron containing iron oxide, iron-containing sludge, or the like, in addition to iron ore containing Fe ₂ O ₃ and Fe ₃ O ₄ as main components. Carbonaceous-containing materials are coal, bituminous material, oil coke, and the like. As coal, in addition to coal for general use, such as coal for coke making, bituminous coal, semianthracite, anthracite, etc. Swelling coal and solvent refined coal such as SRC. As bitumen, coal, such as pitch, soft pitch, middle softening point pitch, hard pitch, petroleum, such as ASP (asphalt pitch), PDA (propane deasphalting asphalt), etc. Examples of petroleum bituminous materials and oil coke include fluid coke and delayed coke.

As an example of the results of various analyzes, Figs. 1 and 2 show the transition of the maximum thermal stress generated inside the molded article when the molded article is heated. Molded products made of 100 mass% of coal as a carbonaceous material as a raw material and a raw material of iron ore 10 mass% of iron oxide and 90 mass% of coal as a carbonaceous material to have a capacity of 18 cc, 50 cc, and 92 cc, respectively. Fig. 1 shows the transition of the maximum thermal stress generated inside the molding when the isothermal gradient is heated at a constant heating rate of 5K (Kelven) / min (5 ° C / min). The case of the molding which mixed 10 mass% of iron ore and 90 mass% of coal is shown in FIG. Thermal stresses also measure the temperature-dependent linear shrinkage coefficient, Young's modulus, specific heat, thermal conductivity, and density of coal and iron oxide-containing coal. Based on these data, the temperature dependence of the thermal stress was calculated by heat transfer and thermal stress calculation. In addition, the linear shrinkage rate is a test sample, which is formed by mixing a predetermined amount of coal and iron oxide into a cylindrical shape having a diameter of 5 mm and a height of 8 mm as a test sample, and using a thermomechanical analyzer. It measured using. The Young's modulus was measured using a resonance method by mixing a predetermined amount of coal and iron oxide and cutting it into a plate having a width of 15 mm, a length of 80 mm, and a thickness of 10 mm as a test sample. Poisson's ratio is also described in J. Fukai, T. Hashida, K. Suzuki, T. Miura and S. Ohtani: Tetsu-to-Hagane, vol. 74 (1988), p. 2209. Based on the specific heat, thermal conductivity and density (K, Matsuba, O. Tajima, N. Suzuki, Y. Okada, Y. Nakayama and T. Kato: Tetsu-to-Hagane, vol. 68 (1982), It measured based on the method described in p.2148). In addition, the above-mentioned electrothermal thermal stress calculation is based on the method (T.Miura, H. Yoshino, S. Saito, S. Otani: Journal of the Fuel Society of Japan, vol. 68 (1989), p. 1045). Was used.

As shown in FIG. 1, when the molded object which consists only of a carbon containing material is carbonized, the peak of a large thermal stress shows in the surface temperature of a molded object near 700 degreeC-750 degreeC. The reason is explained using FIG.

FIG. 5 is a graph showing the temperature dependence of the coefficient of linear contraction of a molded product consisting of 100 mass% of coal, 90 mass% of coal and 10 mass% of iron ore, 70 mass% of coal, and 30 mass% of ore, as shown in FIG. In the heat treatment process of the coal 100mass% molding, a peak (the so-called second peak of the linear shrinkage) is observed around 750 ° C. As described above, when the surface temperature is around 750 ° C., the shrinkage rate of the surface is maximized, whereas the inside of the molded article has a lower temperature than the surface, so the contractile rate is relatively smaller than the surface. As a result, shrinkage difference occurs between the surface and the inside of the molding, so that the probability of crack formation increases. Moreover, the mixed molding of coal and iron ore also shows the secondary peak similarly. In addition, although the peak (the so-called linear shrinkage primary peak) is observed in 500 degreeC vicinity, since the Young's modulus of the coke | molding of 100 mass% of coal is small in this 1st peak temperature range, as shown in FIG. Likewise, the thermal stresses generated are relatively small and are not a problem. As shown in Fig. 1, as the molded article capacity increases, the temperature difference between the surface and the inside of the molded article increases, so that the value of the peak of the maximum thermal stress increases. On the other hand, when the molded product which mixed the iron oxide containing material and the carbon containing material is dried, it shows the linear shrinkage as shown in FIG. 5, and the thermal conductivity of an iron oxide containing material is about 100 times compared with a carbon containing material, for example. Because of their size, the temperature difference between the surface and the inside of the molding becomes smaller compared to only the carbon-containing material. The same tendency is observed even if the content of the iron oxide-containing substance is increased. Therefore, as shown in FIG. 2, in the mixed molding of an iron oxide containing material and a carbon containing material, the peak of thermal stress in the vicinity of 700 to 750 degreeC becomes negligibly small. On the other hand, the surface temperature of a molding shows the peak of a large thermal stress in the vicinity of 550 degreeC-650 degreeC which shows the minimum value from the 1st peak value of a line shrinkage rate. In the case of the carbon-containing substance alone (coal 100mass%: coke), since the Young's modulus is small at this temperature range, the thermal stress was not a problem, but in the case of a molded article (ferrocoke) in which the iron oxide-containing material and the carbon-containing material were mixed, iron oxide Since the Young's modulus increases under the influence of the containing substance, a large thermal stress is generated even at a slight torsional change in this temperature range. Even if the size of the molded product is reduced and the internal temperature distribution is suppressed, the Young's modulus dependence is large. Therefore, the dependency of the molded product capacity becomes small. In addition, in this temperature range, since the bonding strength between the particles composed of the carbon-containing material is low, a slight increase in the generated thermal stress greatly affects crack formation.

As described above, in the mixture of the carbon-containing material and the iron oxide-containing material, the thermal stress generation temperature is different compared to that of the carbon-containing material alone. Therefore, in order to suppress cracking during drying, that is, generation of thermal stress, It was newly discovered that the heating method of 550 ° C to 650 ° C without control was newly completed, and the following invention was completed.

In addition, the following 550 degreeC-650 degreeC heating method used by this invention makes iron oxide containing material content the case of the drying of the molding obtained from hot briquetting in shaping | molding a mixture of a carbon containing material and an iron oxide containing material. It is an effective heating method also at the time of dry distillation of the molding obtained by cold briquetting using a binder in large amounts.

As a method of controlling the heating method of 500 degreeC-650 degreeC, the method of controlling a heating rate is mentioned. The slower the heating rate is, the smaller the temperature difference between the surface of the molded article and the inside of the molded article becomes, so that it is possible to suppress the generation of thermal stress. However, slowing down the heating rate lengthens the drying time, which is not preferable in order to reduce the productivity of the product. Therefore, setting the upper limit of the heating rate is important. Incidentally, the heating rate in the present invention is not the average heating temperature (ΔT / t) obtained by dividing the elevated temperature ΔT ° C by the time t required for the elevated temperature, but the instantaneous heating rate (temperature gradient of the heat pattern (dT / dt) Say).

For example, in FIG. 3, the maximum thermal stress generated inside the molding is 100 mass% of coal as the carbonaceous material, and 10 mass% of iron ore as the iron oxide material and 90 mass% of coal as the carbonaceous material. 4 shows the case where the mixture of is used as a raw material. 3 and 4 respectively show the maximum thermal stress generated inside the molded product when the molded product molded at a capacity of 18 cc is heated at a constant heating rate of 5, 10 and 20 K / min (° C / min). This graph shows the trend of. In the case of any raw material, it can be seen that the maximum thermal stress generated as the heating rate is reduced.

As a result of analyzing the deformation and the cracking condition of the molded product heat-treated under various conditions, the upper limit of the heating rate of 550 to 650 ° C when carbonizing ferrocoke is 20 ° C / min (K / min), which is an instantaneous temperature gradient. By heating at the heating rate of 20 degrees C / min or less, it discovered that hardly a crack generate | occur | produced in the molded object.

In addition, the mass% of the iron oxide containing material in the preferable ferro coke raw material molding of this invention is 10 mass%-30 mass%, and remainder is a carbonaceous-containing substance. The capacity of the preferred ferrocoke raw material moldings of the present invention is at least 6 cc.

≪ Example 1 >

In order to clarify the relationship between the ferrocoke heat treatment conditions and the cracking of the ferrocoke, a heating test of the ferrocoke raw material molding was conducted using an electric furnace whose heating rate can be controlled to investigate the occurrence of cracks.

First, adjustment of the raw material for ferro coke was performed. Two kinds of raw materials are selected: coal (raw coal) with 35 mass% of volatile matter as the carbonaceous material, iron ore with 68 mass% of Fe content as the iron oxide-containing material, and coal and iron ore mixed at a mass ratio of 9: 1 and 7: 3. Ready. Next, three types of molded articles having a capacity of 6 cc, 18 cc, and 50 cc were manufactured using a double roll type molding machine. These moldings were heated in various heat patterns by an electric furnace.

The molded article molded by the above is arranged several times in the soaking area of an electric furnace, and it heats to 900 degreeC by various heating patterns in a nitrogen atmosphere, it cools gradually in a nitrogen atmosphere, and it is room temperature. After cooling, the tube was taken out of the electric furnace and the appearance was observed, and the ratio of the ferro coke (original form ratio) that was in a circular shape was measured. What did not have a crack in the surface of the obtained ferro coke was made into ferro coke only circular.

Table 1 shows the results obtained by arranging the roundness at a constant heating rate when the temperature gradient in the temperature range of 550 to 650 ° C. in the case of a molded article made of coal and iron ore is a raw material having a mass ratio of 7: 3. In addition, the heating rate in temperature ranges other than 550-650 degreeC changes suitably, and is not constant at each heating rate. Also in the case of a molded article composed of coal and iron ore in a mass ratio of 9: 1, the same result as in the case of a molded article composed of coal and iron ore in a mass ratio of 7: 3 was obtained. The result of the molded object which consists of a raw material of 9: 1 mass ratio was abbreviate | omitted.

No crack was found at all when the heating rate of 550-650 degreeC was 10 degrees C / min or less also about the mass ratio of the molded object of any capacity | capacitance and the coal and iron ore of 9: 1 and 7: 3. In addition, at 20 degrees C / min or less, the broken molding was less than 10%, and was confirmed slightly, but it was not enough to affect productivity. On the other hand, when the heating rate was heated at 25 ° C / min or more in excess of 20 ° C / min, apparently many broken ferro cokes were found.

Claims (8)

In the method of manufacturing the ferro coke by carbonizing the molded article formed by mixing the iron oxide containing material and the carbonaceous containing material by heating,
A method for producing ferrocoke, characterized in that the heating rate in the temperature range of the surface temperature of the molded product is 550 to 650 ° C to 5 ° C / minute or more and 20 ° C / minute or less. The method of claim 1,
The said heating rate is 5 degrees C / min or more, 10 degrees C / min or less, The manufacturing method of the ferro coke. The method of claim 1,
The heating rate is 10 ℃ / min or more, 20 ℃ / min or less, characterized in that the ferro coke production method. The method of claim 3, wherein
The said heating rate is 10 degrees C / min or more, 15 degrees C / min or less, The manufacturing method of the ferro coke. The method of claim 3, wherein
The heating rate is 15 ℃ / min or more, 20 ℃ / min or less, characterized in that the ferro coke production method. The method of claim 1,
The ferro coke has a capacity of 6 to 50cc, characterized in that the ferro coke production method. The method according to claim 6,
The ferro coke production method characterized in that the ferro coke has a capacity of 6 to 18cc. The method of claim 1,
The said iron oxide containing material has a content of 10-30 mass% with respect to a molded object, The manufacturing method of the ferro coke characterized by the above-mentioned.

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