摘要:
A fluidized bed reduction reactor has a plurality of fluidized bed reactors (10) with inner gas distributors (19). A charge duct (12) passes through the top of the fluidized bed reactor (10) with a free end to charge a fine iron ore into said reactor (10). The free end of the iron ore charging duct (12) is positioned close to the top center of the gas distributor (19). A spiral-shaped partition weir (13) is placed over the gas distributor and surrounds the iron ore charging duct (12) while being spirally extended to an inner wall of the fluidized bed reactor (10) where it is fixed. The fine iron ore is fluidized and reduced while spirally flowing from the center of the fluidized bed rector (10) to its inner wall. In this structure, the back mixture phenomenon where the reacted fine iron ore is mixed with the non-reacted fine iron ore does not occur.
摘要:
In a method of producing liquid pig iron (43) or liquid steel precursors from charges consisting of iron ore (5) and fluxes, having at least in part a proportion of fines, the iron ore is reduced directly to sponge iron in two or more reduction stages (1, 2) by the fluidized-bed method. The sponge iron is then melted in a smelting-gasification zone (39), with carbonaceous materials and oxygenous gas added; a reducing gas containing CO and H2 is generated, which is introduced into the reducing zones of the reduction stages (1, 2), reacts there, is drawn off as top gas, and supplied to a consumer, where appropriate. In order to achieve uniform reduction of the iron ore with optimum utilization of the reducing gas, in a first reduction stage (1), the iron ore (5) is fractionated into two or more fractions of different grain-size distributions, with the help of the reducing gas; each fraction is reduced with the reducing gas in its own fluidized bed (6, 15); the reducing gas sustaining a first fluidized bed (6), containing the coarse-grain fraction, and separating the fine-grain fraction from it, and additional reducing gas being introduced directly into the other fluidized bed (15); reduced iron ore (5) is withdrawn from both the first and the additional fluidized beds (6, 15), and the fine-grain and coarse-grain fractions reduced in the first reduction stage (1) are reduced further in one or more additional reduction stages (2), that operate in the same way as the first reduction stage (1); from the last reduction stage (2), the fine-grain fraction is fed into the smelting-gasification zone (39) under agglomeration by addition of oxygen, and the coarse-grain fraction is gravity-fed directly into the smelting-gasification zone (39).
摘要:
In a process for the treatment of particulate matter by fluidisation the particulate matter is held and treated in a fluidised bed reactor (1,1', 1'') with the treatment gas flowing from the bottom to the top. To minimise consumption of the treatment gas, and to reduce the entrainement of fines by the treatment gas, particulate matter with a wide ranging grain size distribution and a relative large content of fines is used and the empty pipe flow rate of the treatment gas in the fluidised bed (2) is kept smaller than the flow rate required for the fluidising of the larger particles of the particulate matter. The reduced material is taken via a transport pipe (6) to a melting gasifier (25) where in a melting gasifying zone (26) a reduction gas with CO and H2 content is produced from carbon and oxygen-containing gas which is introduced into the fluidised bed reactor (1'') via a feed pipe (27).
摘要:
The invention relates to a method for producing liquid pig iron (43) or liquid steel precursors from a hardening material formed by iron ore (5) and additives and having at least partially fines. To achieve a uniform reduction of the iron ore with optimum utilization of the reducing gas, the iron ore (5) is fractionated into at least two fractions, each of them having different grain size distribution, during a first reduction stage (1) with the help of the reducing gas. Each fraction is then reduced with the reducing gas in its own fluidized bed, whereby the reducing gas maintains a first fluidized bed (6) containing the coarse grain fraction and separates the fine grain fraction from it. An additional reducing gas is later introduced directly into the other fluidized bed (15). The reduced iron ore (5) is withdrawn both from the first and from the other fluidized bed (6, 15). The fine and coarse grain fractions reduced during the first reduction stage (1) are further reduced in ore or more additional reduction stages (2) operating in the same way as the first reduction stage (1). The fine grain fraction obtained during the last reduction stage (2) is fed into the smelting-gasification zone (39) under agglomeration by adding oxygen. The coarse grain fraction is gravity fed directly into the smelting-gasification zone (39).
摘要:
A fluidized bed reduction reactor has a plurality of fluidized bed reactors (10) with inner gas distributors (19). A charge duct (12) passes through the top of the fluidized bed reactor (10) with a free end to charge a fine iron ore into said reactor (10). The free end of the iron ore charging duct (12) is positioned close to the top center of the gas distributor (19). A spiral-shaped partition weir (13) is placed over the gas distributor and surrounds the iron ore charging duct (12) while being spirally extended to an inner wall of the fluidized bed reactor (10) where it is fixed. The fine iron ore is fluidized and reduced while spirally flowing from the center of the fluidized bed rector (10) to its inner wall. In this structure, the back mixture phenomenon where the reacted fine iron ore is mixed with the non-reacted fine iron ore does not occur.
摘要:
The invention concerns a process for reducing ore fines by means of reducing gas in a fluidized bed process. In order to obtain a homogeneous degree of metallization whilst making optimum use of the reducing gas and minimizing the amount thereof, the following combination of steps is applied: the ore fines (2) are fractionated by means of the reducing gas into at least two fractions each having different grain size distributions; each fraction is reduced in its own fluidized bed (3, 12) with the reducing gas; the reducing gas maintains a first fluidized bed (3) containing the coarse grain fraction and separates therefrom the fine grain fraction, it is then accelerated together with the fine grain fraction and subsequently, as it expands, forms a further fluidized bed (12), the gas being continuously fed from below into the further fluidized bed (12) in a radial symmetrical manner; a secondary reducing gas is introduced directly in a radial symmetrical manner into the further fluidized bed (12); and reduced ore is discharged both from the first and the further fluidized bed (3, 12).
摘要:
The invention concerns a process for reducing ore fines by means of reducing gas in a fluidized bed process. In order to obtain a homogeneous degree of metallization whilst making optimum use of the reducing gas and minimizing the amount thereof, the following combination of steps is applied: the ore fines (2) are fractionated by means of the reducing gas into at least two fractions each having different grain size distributions; each fraction is reduced in its own fluidized bed (3, 12) with the reducing gas; the reducing gas maintains a first fluidized bed (3) containing the coarse grain fraction and separates therefrom the fine grain fraction, it is then accelerated together with the fine grain fraction and subsequently, as it expands, forms a further fluidized bed (12), the gas being continuously fed from below into the further fluidized bed (12) in a radial symmetrical manner; a secondary reducing gas is introduced directly in a radial symmetrical manner into the further fluidized bed (12); and reduced ore is discharged both from the first and the further fluidized bed (3, 12).