Evaluation of the Limiting Regime in Iron Ore Fines Reduction with H2-Rich Gases in Fluidized Beds: Fe2O3 to Fe3O4
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in: Chemical Engineering & Technology, Jahrgang 32.2009, Nr. 3, 25.02.2009, S. 392-397.
Publikationen: Beitrag in Fachzeitschrift › Artikel › Forschung › (peer-reviewed)
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TY - JOUR
T1 - Evaluation of the Limiting Regime in Iron Ore Fines Reduction with H2-Rich Gases in Fluidized Beds: Fe2O3 to Fe3O4
AU - Sturn, Johannes
AU - Voglsam, Severin
AU - Weiss, Bernd
AU - Schenk, Johannes
AU - Winter, Franz
PY - 2009/2/25
Y1 - 2009/2/25
N2 - In metallurgical processes, fluidized-bed technology is gaining more importance because of its advantages. Processes with H2-rich and CO-rich reducing gases were developed for the reduction of iron ore fines (e.g. FINEX®). For improvement of these new technologies, greater knowledge about the chemical kinetics of iron ore reduction in fluidized beds is necessary. The scope of this work is to evaluate the limiting regime of the iron ore fines reduction. Therefore, experimental results of reduction tests were compared with theoretically investigated reduction rates. These reduction rates were based on a limitation either of mass transfer through the external gas film to the particle surface, diffusion in a porous product layer (pore diffusion and Knudsen diffusion), diffusion in a dense product layer (solid diffusion) or the phase boundary reaction. The phase boundary reaction was found to be the most likely limiting reaction regime.
AB - In metallurgical processes, fluidized-bed technology is gaining more importance because of its advantages. Processes with H2-rich and CO-rich reducing gases were developed for the reduction of iron ore fines (e.g. FINEX®). For improvement of these new technologies, greater knowledge about the chemical kinetics of iron ore reduction in fluidized beds is necessary. The scope of this work is to evaluate the limiting regime of the iron ore fines reduction. Therefore, experimental results of reduction tests were compared with theoretically investigated reduction rates. These reduction rates were based on a limitation either of mass transfer through the external gas film to the particle surface, diffusion in a porous product layer (pore diffusion and Knudsen diffusion), diffusion in a dense product layer (solid diffusion) or the phase boundary reaction. The phase boundary reaction was found to be the most likely limiting reaction regime.
KW - Fluidized beds
KW - H-rich gases
KW - Iron ore reduction
UR - http://www.scopus.com/inward/record.url?scp=65549152510&partnerID=8YFLogxK
U2 - 10.1002/ceat.200800579
DO - 10.1002/ceat.200800579
M3 - Article
VL - 32.2009
SP - 392
EP - 397
JO - Chemical Engineering & Technology
JF - Chemical Engineering & Technology
SN - 0930-7516
IS - 3
ER -