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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Hessels, Conrad
Eindhoven University of Technology
in Cooperation with on an Cooperation-Score of 37%
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Publications (5/5 displayed)
- 2023Minimum fluidization velocity and reduction behavior of combusted iron powder in a fluidized bedcitations
- 2023Sintering behavior of combusted iron powder in a packed bed reactor with nitrogen and hydrogencitations
- 2022Phase transformations and microstructure evolution during combustion of iron powdercitations
- 2022Reactiekinetiek van verbrand ijzerpoeder met waterstof ; Reduction kinetics of combusted iron powder using hydrogencitations
- 2022Reduction kinetics of combusted iron powder using hydrogencitations
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article
Minimum fluidization velocity and reduction behavior of combusted iron powder in a fluidized bed
Abstract
The fluidization and reduction behavior of micron-sized iron oxide powder, produced by iron combustion, is studied in a lab-scale cylindrical fluidized bed. The minimum fluidization velocity u mf is found to stabilize above normalized static bed heights of 0.5 H/D (static bed height divided by the bed diameter). u mf is measured as a function of temperature between 280 and 860 K for both H 2 and N 2 as fluidizing gas. The experimental results start to deviate from the Ergun correlation at temperatures above 560 K, both for N 2 and H 2 . A new correlation, taking the cohesive inter-particle solid bridge force into account, is proposed in this work to predict the minimum fluidization velocity at high temperature. Reduction experiments are carried out for a total time of 5 h at constant excess velocity with 50, 75 and 100 vol% of H 2 and temperatures between 623 and 823 K. Gradual defluidization occurs when the operating temperature exceeds 800 K. A maximum reduction degree of 61% is obtained at 807 K and 100 vol% H 2 .