Biomass direct reduced iron
US-2023407423-A1 · Dec 21, 2023 · US
US2026043102A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2026043102-A1 |
| Application number | US-202219100439-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 1, 2022 |
| Priority date | Aug 1, 2022 |
| Publication date | Feb 12, 2026 |
| Grant date | — |
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Non-fired pellets are used in a solid reduction furnace and are effective in preventing clustering by reducing the possibility of contact between low-melting-temperature slags and thus preventing the fusion therebetween. A method produces such non-fired pellets. Non-fired pellets for reduction, in which the proportion of high-viscosity slag components (Al 2 O 3 +MgO+SiO 2 ) to the total Fe (T.Fe) satisfies an expression: (Al 2 O 3 +MgO+SiO 2 )/T.Fe≥0.12, and a method for producing the same. In the expression, Al 2 O 3 represents the concentration (mass %) of Al 2 O 3 in the non-fired pellets, MgO represents the concentration (mass %) of MgO in the non-fired pellets, SiO 2 represents the concentration (mass %) of SiO 2 in the non-fired pellets, and T.Fe represents the concentration (mass %) of T.Fe in the non-fired pellets.
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1 . Non-fired pellets for reduction, wherein a proportion of high-viscosity slag components (Al 2 O 3 +MgO+SiO 2 ) to total Fe (T.Fe) satisfies the following Expression (1): ( Al 2 O 3 + MgO + SiO 2 ) / T · Fe ≥ 0 .12 , ( 1 ) where Al 2 O 3 represents a concentration (mass %) of Al 2 O 3 in the non-fired pellets, MgO represents a concentration (mass %) of MgO in the non-fired pellets, SiO 2 represents a concentration (mass %) of SiO 2 in the non-fired pellets, and T.Fe represents a concentration (mass %) of T.Fe in the non-fired pellets. 2 . Non-fired pellets for reduction, wherein a proportion of high-viscosity slag components (Al 2 O 3 +MgO+SiO 2 ) to total Fe (T.Fe) satisfies the following Expression (2): ( Al 2 O 3 + MgO + SiO 2 ) / T · Fe ≥ 0 .15 , ( 2 ) where Al 2 O 3 represents a concentration (mass %) of Al 2 O 3 in the non-fired pellets, MgO represents a concentration (mass %) of MgO in the non-fired pellets, SiO 2 represents a concentration (mass %) of SiO 2 in the non-fired pellets, and T.Fe represents a concentration (mass %) of T.Fe in the non-fired pellets. 3 . A method for producing the non-fired pellets for reduction according to claim 1 , further comprising using an iron-containing raw material formulated to achieve an average LOI (Loss on Ignition) of 5% or more. 4 . The method for producing the non-fired pellets for reduction according to claim 3 , wherein the iron-containing raw material has been pretreated for removal of crystal water in advance so as to achieve an average LOI (Loss on Ignition) of 2% or less. 5 . The method for producing the non-fired pellets for reduction according to claim 3 , wherein a mixed raw material containing 4 mass % to 24 mass % M.Fe is prepared by mixing a raw material containing M.Fe and is granulated. 6 . The method for producing the non-fired pellets for reduction according to claim 5 , wherein the raw material is reduced iron with a particle size of 3 mm or less that has been reduced in a solid reduction furnace. 7 . The method for producing the non-fired pellets for reduction according to claim 6 , wherein the reduced iron contains 79 mass % or more M.Fe. 8 . A method for producing the non-fired pellets for reduction according to claim 2 , further comprising using an iron-containing raw material formulated to achieve an average LOI (Loss on Ignition) of 5% or more. 9 . The method for producing the non-fired pellets for reduction according to claim 8 , wherein the iron-containing raw material has been pretreated for removal of crystal water in advance so as to achieve an average LOI (Loss on Ignition) of 2% or less. 10 . The method for producing the non-fired pellets for reduction according to claim 4 , wherein a mixed raw material containing 4 mass % to 24 mass % M.Fe is prepared by mixing a raw material containing M.Fe and is granulated. 11 . The method for producing the non-fired pellets for reduction according to claim 8 , wherein a mixed raw material containing 4 mass % to 24 mass % M.Fe is prepared by mixing a raw material containing M.Fe and is granulated. 12 . The method for producing the non-fired pellets for reduction according to claim 9 , wherein a mixed raw material containing 4 mass % to 24 mass % M.Fe is prepared by mixing a raw material containing M.Fe and is granulated. 13 . The method for producing the non-fired pellets for reduction according to claim 10 , wherein the raw material is reduced iron with a particle size of 3 mm or less that has been reduced in a solid reduction furnace. 14 . The method for producing the non-fired pellets for reduction according to claim 11 , wherein the raw material is reduced iron with a particle size of 3 mm or less that has been reduced in a solid reduction furnace. 15 . The method for producing the non-fired pellets for reduction according to claim 12 , wherein the raw material is reduced iron with a particle size of 3 mm or less that has been reduced in a solid reduction furnace. 16 . The method for producing the non-fired pellets for reduction according to claim 13 , wherein the reduced iron contains 79 mass % or more M.Fe. 17 . The method for producing the non-fired pellets for reduction according to claim 14 , wherein the reduced iron contains 79 mass % or more M.Fe. 18 . The method for producing the non-fired pellets for reduction according to claim 15 , wherein the reduced iron contains 79 mass % or more M.Fe.
Rotary hearth-type furnaces · CPC title
Use of special additives or fluxing agents · CPC title
making metallised agglomerates or iron oxide · CPC title
pelletizing · CPC title
Recycling · CPC title
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