FIRED PELLETS FOR REDUCTION AND METHOD FOR PRODUCING SAME

Abstract

Fired pellets for use in a solid reduction furnace that are effective in preventing clustering by reducing the possibility of contact between low-melting-temperature slags and thus preventing the fusion therebetween, and a method for producing such fired pellets. Fired pellets for reduction, wherein the proportion of high-viscosity slag components (Al.sub.2O.sub.3+MgO+SiO.sub.2) to the total Fe (T.Fe) satisfies an expression: (Al.sub.2O.sub.3+MgO+SiO.sub.2)/T.Fe0.09, and a method for producing the same. In the expression, Al.sub.2O.sub.3 represents the concentration (mass %) of Al.sub.2O.sub.3 in the fired pellets, MgO represents the concentration (mass %) of MgO in the fired pellets, SiO.sub.2 represents the concentration (mass %) of SiO.sub.2 in the fired pellets, and T.Fe represents the concentration (mass %) of T.Fe in the fired pellets.

Claims

1. Fired pellets for reduction, wherein a proportion of high-viscosity slag components (Al.sub.2O.sub.3+MgO+SiO.sub.2) to total Fe (T.Fe) satisfies the following Expression (1): $\begin{array}{cc}\left({\mathrm{Al}}_2{O}_3+\mathrm{MgO}+{\mathrm{SiO}}_2\right)/T.\mathrm{Fe}0.09,& \left(1\right)\end{array}$ where Al.sub.2O.sub.3 represents a concentration (mass %) of Al.sub.2O.sub.3 in the fired pellets, MgO represents a concentration (mass %) of MgO in the fired pellets, SiO.sub.2 represents a concentration (mass %) of SiO.sub.2 in the fired pellets, and T.Fe represents a concentration (mass %) of T.Fe in the fired pellets.

2. Fired pellets for reduction, wherein a proportion of high-viscosity slag components (Al.sub.2O.sub.3+MgO+SiO.sub.2) to total Fe (T.Fe) satisfies the following Expression (2): $\begin{array}{cc}\left({\mathrm{Al}}_2{O}_3+\mathrm{MgO}+{\mathrm{SiO}}_2\right)/T.\mathrm{Fe}0.12,& \left(2\right)\end{array}$ where Al.sub.2O.sub.3 represents a concentration (mass %) of Al.sub.2O.sub.3 in the fired pellets, MgO represents a concentration (mass %) of MgO in the fired pellets, SiO.sub.2 represents a concentration (mass %) of SiO.sub.2 in the fired pellets, and T.Fe represents a concentration (mass %) of T.Fe in the fired pellets.

3. The fired pellets for reduction according to claim 1, wherein a porosity is 20% or more.

4. The fired pellets for reduction according to claim 1, wherein a porosity is 30% or more.

5. A method for producing the fired pellets for reduction according to claim 1, wherein reduction and firing are performed by using an iron-containing raw material formulated to achieve an average LOI (Loss on Ignition) of 5% or more.

6. The method for producing the fired pellets for reduction according to claim 5, wherein the iron-containing raw material has been subjected to a crystal water removal pretreatment in advance so as to achieve an average LOI (Loss on Ignition) of 2% or less.

7. The method for producing the fired pellets for reduction according to claim 6, wherein the crystal water removal pretreatment comprises heating and drying using a rotary kiln and using a measurement value of a sample at the exit side of the kiln as the average LOI (Loss on Ignition) of the iron-containing raw material.

8. The method for producing the fired pellets for reduction according to claim 5, wherein a mixed raw material containing 4 mass % to 24 mass % M.Fe is prepared by mixing a raw material containing M.Fe, and the mixed raw material is granulated and fired.

9. The method for producing t fired pellets for reduction according to claim 8, wherein the raw material is reduced iron having a particle size of 3 mm or less that has been reduced in a solid reduction furnace.

10. The method for producing the fired pellets for reduction according to claim 9, wherein the reduced iron contains 78 mass % or more M.Fe.

Description

BRIEF DESCRIPTION OF DRAWING

[0033] FIG. 1 is a graph illustrating the relationship between (Al.sub.2O.sub.3+MgO+SiO.sub.2)/T.Fe and LOI of Australian iron ore that is an iron-containing raw material to be mixed.

DESCRIPTION OF EMBODIMENTS

[0034] A solid reduction furnace used in the present invention is a furnace for reducing fed fired pellets for reduction to Fe having a reduction degree of 90% or more by using a hydrogen gas, etc., as a reducing gas. In the operation of such a solid reduction furnace, the properties of raw material fed into the furnace, that is, the fired pellets are important.

[0035] What is most important for the fired pellets is whether the pellets can be prevented from contacting or fusing with each other, which would otherwise result in clustering, in a high-temperature zone (500 to 800 C.) of the solid reduction furnace as described above. In response to such demand, in the present invention, studies have been made on the relationship between an iron-containing raw material such as metallic iron, iron oxide such as iron ore, iron sulfide, or ironmaking dust and high-viscosity slag components. As a result, from the viewpoint of the fluidity of the various raw materials in the furnace, it is found preferable to appropriately manage the relationship particularly between the iron-containing raw material and high-viscosity slag components. That is, the high-viscosity slag is always controlled to be generated in the furnace so that an undesirable flow in the high-temperature zone is suppressed. This can prevent the fusion between slags, thereby preventing clustering.

[0036] As described previously, in the present invention, it has been found to be effective to include the high-viscosity slag components in a given ratio in an iron-containing raw material, iron ore, or an auxiliary material to be mixed.

[0037] As the components that can be the high-viscosity slag, focus is placed on (Al.sub.2O.sub.3, MgO, and SiO.sub.2), in particular. When the total content of such components is maintained at a predetermined ratio relative to the total iron (T.Fe), it becomes possible to effectively prevent the slag-to-slag fusion caused in the furnace.

[0038] This can be achieved when the fired pellets for reduction have a component composition such that the high-viscosity slag components (Al.sub.2O.sub.3+MgO+SiO.sub.2) are contained in a given ratio relative to the total iron (T.Fe) in the iron-containing raw material. That is, when the fired pellets satisfy the relationship of Expression (1) below.

[00003]$\begin{array}{cc}\left({\mathrm{Al}}_2{O}_3+\mathrm{MgO}+{\mathrm{SiO}}_2\right)/T.\mathrm{Fe}0.09,& \left(1\right)\end{array}$

[0039] In Expression (1) above, Al.sub.2O.sub.3 represents the concentration (mass %) of Al.sub.2O.sub.3 in the fired pellets for reduction. MgO represents the concentration (mass %) of MgO in the fired pellets for reduction. SiO.sub.2 represents the concentration (mass %) of SiO.sub.2 in the fired pellets for reduction. T.Fe represents the total Fe concentration (mass %) in the fired pellets for reduction.

[0040] In the present invention, there exists a more preferable relationship between the high-viscosity slag components (Al.sub.2O.sub.3+MgO+SiO.sub.2) and the total iron (T.Fe) from the viewpoint of preventing the contact or fusion between the slags in the high-temperature range of the furnace, which is Expression (2) below. The relationship indicates that the high-viscosity slag components are contained in a higher amount.

[00004]$\begin{array}{cc}\left({\mathrm{Al}}_2{O}_3+\mathrm{MgO}+{\mathrm{SiO}}_2\right)/T.\mathrm{Fe}0.12& \left(2\right)\end{array}$

[0041] In Expression (2) above, Al.sub.2O.sub.3 represents the concentration (mass %) of Al.sub.2O.sub.3 in the fired pellets for reduction. MgO represents the concentration (mass %) of MgO in the fired pellets for reduction. SiO.sub.2 represents the concentration (mass %) of SiO.sub.2 in the fired pellets for reduction. T.Fe represents the total Fe concentration (mass %) in the fired pellets for reduction.

[0042] Note that in the present invention, the total Fe in the iron-containing raw material refers to the total value of the iron concentrations including the concentrations of metallic iron (M.Fe) and iron compounds (iron oxide, iron sulfide, calcium ferrite, etc.). Meanwhile, the high-viscosity slag components refer to the total value of the concentrations of Al.sub.2O.sub.3, MgO, and SiO.sub.2 contained in the iron-containing raw material, such as iron ore or ironmaking dust; an auxiliary material (limestone, quicklime, dolomite, etc.); and a binder (bentonite, etc.).

[0043] The Al.sub.2O.sub.3, MgO, and SiO.sub.2 concentrations can be determined as follows. First, the Al concentration, Mg concentration, and Si concentration are measured by elemental analysis such as fluorescent X-ray analysis, for example. Then, each oxide concentration can be determined by multiplying the element concentration thus determined by (the molecular weight of the oxide per element/atomic weight). Specifically, for example, the Al.sub.2O.sub.3 concentration can be determined by multiplying the Al concentration measured by elemental analysis, such as fluorescent X-ray analysis, by (the Al.sub.2O.sub.3 molecular weight/2)/the Al atomic weight=50.98/26.98=1.890.

[0044] It is also critical to control the porosity of the fired pellets for reduction according to the present invention, That is, when the fired pellets for reduction are made porous (20% or more, preferably 30% or more), the number of contact points between the pellets can be reduced, which can also reduce the contact between metallic irons and prevent fusion, thereby contributing to the prevention of the clustering described above. In this respect, a porosity of less than 20% is not effective in preventing fusion. The upper limit is approximately 60% from the viewpoint of strength.

[0045] Next, the method for producing the fired pellets according to the present invention will be described. When producing the fired pellets for reduction according to the present invention, in order for the fired pellets to satisfy the above relationship between the high-viscosity slag components (Al.sub.2O.sub.3+MgO+SiO.sub.2) and the total iron (T.Fe), for example, it is possible to use an iron ore originally having a composition of components satisfying the above relationship, or to selectively use and mix a plurality of iron ores to satisfy the above relationship. For example, one or more of iron ores (brands) shown in FIG. 1, which are Australian iron ores, may be mixed, followed by granulation with a binder, such as bentonite, and an auxiliary material, such as quicklime, added thereto as appropriate.

[0046] When feeding the above fired pellets into the solid reduction furnace and reducing the pellets therein it is critical that these pellets do not have properties that would cause clustering in a high-temperature reducing atmosphere in the furnace. Therefore, in the present invention, focus is placed particularly on LOI (Loss on Ignition), the appropriate value of which has been studied. That is, in the production method according to the present invention, some of the types of iron ore (A to Z) shown in FIG. 1 are selectively used (mixed) to achieve a LOI (Loss on Ignition) value of 5% or more so that LOI5% is satisfied, thereby reducing clustering more effectively. This is because when volatile components, such as crystal water, in the pellets are dissociated and vaporized in the firing process for pellets, and then dissipate to the outside of the pellets, the volume of the mineral phases remaining in the pellets is reduced, resulting in voids between the adjacent mineral phases.

[0047] Next, in the production method according to the present invention, for the iron-containing raw material to achieve the relation LOI5%, it is preferable to apply a pretreatment such as a process for removing crystal water to the iron ore to be used in advance so as to achieve LOI2%. Since many iron-containing raw materials such as raw material iron ore have a high crystal water content, pellets often burst during granulation due to water vapor generated from the crystal water. Thus, it would be unavoidable to increase the temperature slowly. This would reduce productivity.

[0048] In the pretreatment such as a process for removing crystal water, it is preferable to use values measured at the exit side of the granulator such as rotary kiln for LOI evaluation.

EXAMPLES

Embodiment 1

[0049] The Examples (including Comparative Examples) show how the relationship between T.Fe and high-viscosity slag components (Al.sub.2O.sub.3+MgO+SiO.sub.2) in fired pellets for reduction affects the clustering in a solid reduction furnace.

[0050] As the iron-containing raw material, i.e. iron ore used herein, mainly one or more types of Australian iron ores (A to Z) shown in FIG. 1 were mixed with an auxiliary material and reagent (e.g., commercially available Al.sub.2O.sub.3 reagent) as appropriate. Table 1 shows examples of the component compositions of the mixtures.

[0051] All raw materials including one or more types of the Australian raw materials described above (exemplified in FIG. 1) (A to Z) were ground in a ball mill and then granulated with a pelletizer while adding water to achieve a size of 9 to 16 mm. Then, the pellets after granulation were placed in a dryer to perform drying treatment at 110 C. for 24 hr. The pellets were then fed into an electric furnace to be heated at 7 C./min., held at 1250 C. for 10 hr, and then cooled at 7 C./min. Each of the fired pellets obtained, shown in Table 1, was evaluated using a porosity and a clustering index.

(Clustering Evaluation Test)

[0052] A sample weighing 500 g was fed into a vertical cylindrical furnace with a diameter of 100 mm and heated to 1000 C. in an N.sub.2 atmosphere. When the temperature of the sample reached 1000 C., a reducing gas was introduced into the furnace at a rate of 24 NL/min. The composition of the reducing gas was set to a volume ratio of H.sub.2:N.sub.2=20:80. The sample was then loaded at a rate of 1 kg/cm.sup.2 and held in this state for three hours, followed by cooling in an N.sub.2 atmosphere, so that reduced iron was produced. The reduced iron obtained was then sieved through a 16 mm sieve mesh, which is the maximum size of a single fired pellet, to measure the weight Wa (g) of the fired pellets remaining on the sieve. The fired pellets remaining on the sieve were put into a cylindrical shape vessel (132 mm700 mmL) of an I-type testing machine and were rotated at a rotational speed of 30 rpm for five minutes, to measure the weight Wb (g) of the fired pellets remaining on the sieve mesh of 16 mm. The fired pellets were evaluated based on a clustering index that is proportional to the non-crushing clustering proportion Wb/Wa.

(Porosity)

[0053] The porosity of the fired pellets was evaluated by measuring the apparent density of the pellets and then measuring the real density of the pellets. As shown in Table 1, it is confirmed that each of the fired pellets of Examples 1 to 5 in which (Al.sub.2O.sub.3+MgO+SiO.sub.2)/T.Fe is 0.09 or more has a clustering index of less than 7, and thus has excellent properties.

TABLE-US-00001 TABLE 1 LOI (%) of Iron Ore (Al.sub.2O.sub.3 + Poros- Clus- Before MgO + SiO.sub.2)/ ity tering Firing TFe (vol %) Index Comparative Example 1 0.3 0.03 13 52 Comparative Example 2 0.4 0.07 8 25 Example 1 5.1 0.09 22 7 Example 2 7.2 0.12 20 0 Example 3 8.8 0.18 23 0 Example 4 9.1 0.09 33 0 Example 5 10.3 0.09 49 0

[0054] Note that Table 2 below shows the component compositions of the fired pellets obtained in Examples 1 and 2 of Table 1.

TABLE-US-00002 TABLE 2 (mass %) T.Fe FeO SiO.sub.2 CaO Al.sub.2O.sub.3 MgO C/S Example 1 64.9 0.2 3.1 1.2 2.7 0.2 0.4 Example 2 62.5 0.4 4.9 2.9 2.3 0.3 0.6

Embodiment 2

[0055] Next, an evaluation test was conducted to determine whether granulation and firing can be achieved without breakage during granulation, by subjecting the sample in Example 5, shown in Table 1, to a crystal water removal pretreatment. It should be noted that the heating rate was set at 200 C./min.

[0056] The result shows that breakage would be caused, when, for example, a number of pores remains in the ores with crystal water removed, rather than when crystal water was removed by the crystal water removal treatment. Meanwhile, breakage would not be caused when the crystal water removal treatment was sufficiently completed, and furthermore, as long as the LOI of the ore before the treatment was sufficiently high, it is possible to produce good quality pellets even if the LOI of the ore after the crystal water removal treatment was low.

TABLE-US-00003 TABLE 3 LOI (%) of Iron Ore After Crystal Water Porosity Removal Treatment Results (%) Comparative Example 3 10.3 Breakage Comparative Example 4 5.2 Breakage Example 6 2 Satisfactory 45 Example 7 0.7 Satisfactory 43

Embodiment 3

[0057] Reduced iron (a sample when Wa was measured) obtained by the same method as the method of Comparative Example 2 in Embodiment 1 (clustering evaluation test) was ground into particles with a size of 3 mm or less. The resulting particles were mixed with the unfired raw material of Comparative Example 2. The mixture was used to produce fired pellets by the method of Embodiment 1. The crushing strength of the resulting fired pellets was then measured. The measurement results are shown in Table 4.

[0058] In Table 4, M.Fe is derived from metallic iron (M.Fe) contained in the reduced iron. In Examples 10 to 12, reduced iron containing M.Fe=78 mass % was used. In Example 13, reduced iron containing M.Fe=80 mass % was used. As a result, it was found that mixing M.Fe with the raw material can increase the strength of the resulting pellets. Since clustering is promoted as the amount of powder increases, it is possible to suppress clustering by increasing the strength of the fired pellets. The reason why mixing M.Fe with the raw material can increase the strength of the resulting fired pellets is considered that reduced iron powder is oxidized and generates heat when the pellet is fired, thus promoting fusion between adjacent particles.

TABLE-US-00004 TABLE 4 Pellet MFe (Al.sub.2O.sub.3 + Strength (mass %) MgO + SiO.sub.2)/TFe (kgf) Comparative Example 2 0 0.07 178 Example 10 4 0.07 218 Example 11 8 0.07 221 Example 12 24 0.07 233 Example 13 8 0.09 255

[0059] In this specification, the unit L of volume represents 10.sup.3 m.sup.3. Symbol N added to the unit of the volume of a gas represents the volume of the gas in the standard state, that is, at a temperature of 0 C. and a pressure of 101325 Pa. The unit rpm of a rotational speed represents the number of rotations per min.

INDUSTRIAL APPLICABILITY

[0060] The fired pellets for solid reduction according to the present invention are the method that has been developed to be mainly applied to a hydrogen-based direct reduction process, for example. However, as a matter of course, such fired pellets can also be used as a raw material for use in a blast furnace, etc.