A method for producing sintered ore
A technology of sintering and sintering and returning ore, which is applied in the field of sintering and agglomeration, can solve the problems of high cost, increased dependence on iron ore resources, and insufficient recycling and utilization, and achieve the effect of low cost and reduced dependence
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example 1
[0035] Material selection step; wet dust removal sludge composition: TFe% 56.58, FeO% 30.86, SiO 2 %1.83, Al 2 o 3 %0.66, Fe 2 o 3 % 27.12, CaO% 11.93, MgO% 3.9, MnO% 1.2, P 2 o 5 %0.1, S%0.078, metal Fe%13.59; dry dust removal ash composition: TFe%58.17, FeO%12.58, SiO 2 %2.01, Al 2 o 3 %0.099, Fe 2 o 3 %60.04, CaO%5.82, MgO%0.9, MnO%0.81, P 2 o 5 % 0.1, S% 0.048, metal Fe% 5.58; blast furnace gravity dust composition: TFe% 46.07, C% 23.05, CaO% 6.50, SiO 2 %6.01; Lime powder under sieve SiO 2 %0.70, S%0.004, MgO%0.72, CaO%85.00; coke powder Ad%12.65, Vdaf%1.30, St%0.79.
[0036] Batching steps; this example 1 uses all solid secondary resources, in which converter wet dedusting sludge accounts for 46% of all sintering raw materials, converter dry dedusting ash accounts for 20% of all sintering raw materials, and converter dedusting solid waste accounts for 66% of all sintering raw materials %, blast furnace gravity dedusting ash accounts for 10% of the total sin...
example 2
[0047] Material selection step; wet dust removal sludge composition: TFe% 60.97, FeO% 31.19, SiO 2 %1.98, Al 2 o 3 %1.74, Fe 2 o 3 % 30.06, CaO% 6.11, MgO% 2.28, MnO% 1.70, P 2 o 5 %0.128, S%0.078, metal Fe%15.67; dry dust removal ash composition: TFe%60.00, FeO%32.43, SiO 2 %1.70, Al 2 o 3 %0.132, Fe 2 o 3 % 25.01, CaO% 7.6, MgO% 0.79, MnO% 0.81, P 2 o 5 % 0.087, S% 0.037, metal Fe% 17.27; blast furnace gravity dust composition: TFe% 41.54, C% 24.12, CaO% 5.03, SiO 2 %6; sieved limestone powder SiO 2 % 1.08, S% 0.0038, MgO% 0.89, CaO% 47.58; coke powder Ad% 12.67, Vdaf% 1.25, St% 0.79.
[0048] Batching step: Example 2 of the present invention uses all solid secondary resources, wherein converter wet dedusting sludge accounts for 43% of the total sintering raw materials, converter dry dedusting ash accounts for 20% of the total sintering raw materials, and converter dedusting solid waste accounts for the proportion of all sintering raw materials 63%, blast furna...
example 3
[0058] Material selection step; wet dust removal sludge composition: TFe% 57.67, FeO% 33.19, SiO 2 %1.67, Al 2 o 3 %1.03, Fe 2 o 3 % 29.17, CaO% 11.57, MgO% 3.3, MnO% 1.6, P 2 o 5 % 0.11, S% 0.086, metal Fe% 8.03; components after dry dust removal: TFe% 59.28, FeO% 10.93, SiO 2 %2.05, Al 2 o 3 %1.03, Fe 2 o 3 %65.01, CaO%5.63, MgO%3.3, MnO%1.6, P 2 o 5 % 0.16, S% 0.078, metal Fe% 5.02; blast furnace gravity dust composition: TFe% 42.09, C% 21.85, CaO% 5, SiO 2 %6.17; lime powder SiO 2 %0.78, S%0.004, MgO%0.72, CaO%93.81; coke powder Ad%12.72, Vdaf%1.29, St%0.80.
[0059] Batching step: Example 3 of the present invention uses all solid secondary resources, wherein converter wet dedusting sludge accounts for 47% of the total sintering raw materials, converter dry dedusting ash accounts for 20% of the total sintering raw materials, and converter dedusting solid waste accounts for the proportion of all sintering raw materials 67%, blast furnace gravity dedusting ash ...
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