Carbon composite agglomerate for producing reduced iron and method for producing reduced iron using the same
Abstract
Provided is a carbon composite briquette which is used as the raw material of a movable hearth furnace for producing reduced iron having a sufficient carbon content and a higher crushing strength, and also provided is a method for producing reduced iron using the carbon composite briquette. The carbon composite briquette for producing reduced iron has a total SiO 2 +Al 2 O 3 +CaO+MgO content that is between 7 and 15 mass %; an MgO content that is between 0.1 and 6 mass %; an Al 2 O 3 /SiO 2 mass ratio that is between 0.34 and 0.52; a CaO/SiO 2 mass ratio that is between 0.25 and 2.0; and a C content such that between 1 and 9 mass % of C is retained in the resulting reduced iron.
Claims
exact text as granted — not AI-modified1 : A carbon composite agglomerate comprising C, Fe, SiO 2 , Al 2 O 3 , CaO, and MgO,
wherein: a total content of SiO 2 , Al 2 O 3 , CaO, and MgO is 7 to 15 mass %, a MgO content is 0.1 to 6 mass %, a mass ratio range of Al 2 O 3 /SiO 2 is 0.34 to 0.52, a mass ratio range of CaO/SiO 2 is 0.25 to 2.0, and wherein the C content is such that 1 to 9 mass % of C remains in reduced iron produced from the carbon composite agglomerate after the agglomerate has been reduced in a moving hearth furnace.
2 : The agglomerate of claim 1 having a porosity of 37.5% or less.
3 : The agglomerate of claim 1 , wherein an average grain size d50 of a carbonaceous material in the agglomerate measured by a laser diffraction scattering grain size distribution measurement method is 30 μm or less.
4 : The agglomerate of claim 1 , further comprising an ironmaking dust.
5 : A method for producing reduced iron by reducing the agglomerate of claim 1 , the method comprising heating the agglomerate with a moving hearth furnace, wherein the moving hearth furnace is divided into a plurality of zones in a moving direction of a hearth, and a final zone of the plurality of zones has an oxidizing atmosphere, to obtain reduced iron comprising 1 to 9 mass % C.
6 : The method of claim 5 , wherein the oxidizing atmosphere of the final zone has a gas oxidation degree OD of 1.0 or more, wherein
OD=(CO 2 +H 2 O+2O 2 )/(CO 2 +H 2 O+O 2 +CO+H 2 ) [where a unit of CO 2 , H 2 O, O 2 , CO, and H 2 is vol %].
7 : The agglomerate of claim 1 , wherein a mass ratio range of CaO/SiO 2 is 0.25 to 1.5.
8 : The agglomerate of claim 1 , wherein a mass ratio range of CaO/SiO 2 is 0.25 to 1.0.
9 : The agglomerate of claim 1 , wherein the C content is such that 4 to 9 mass % of C remains in reduced iron produced from the carbon composite agglomerate after the agglomerate has been reduced in a moving hearth furnace.
10 : The agglomerate of claim 9 having a porosity of 37.5% or less.
11 : The agglomerate of claim 1 having a porosity of 25% to 37.5%.
12 : The agglomerate of claim 9 having a porosity of 25% to 37.5%.
13 : The agglomerate of claim 1 , wherein an average grain size d50 of a carbonaceous material in the agglomerate measured by a laser diffraction scattering grain size distribution measurement method is 10 μm or less.
14 : The agglomerate of claim 1 , in briquette form.
15 : The agglomerate of claim 1 , in pellet form.
16 : The method of claim 5 , wherein the moving hearth furnace is a rotary hearth furnace.
17 : The method of claim 5 , wherein the moving hearth furnace is a straight hearth furnace.
18 : The agglomerate of claim 14 , wherein a crushing strength of the reduced iron is at least 180 kgf/briquette.
19 : The agglomerate of claim 14 , wherein a crushing strength of the reduced iron is at least 300 kgf/briquette.
20 : The agglomerate of claim 14 , wherein a crushing strength of the reduced iron is at least 600 kgf/briquette.Cited by (0)
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