Hydrogen reduction of combusted iron powder: Role of the fluidization regime on the conversion

Fluidized bed systems play a crucial role in industrial processes such as combustion and gasification. In the Iron Power Cycle, fluidized bed systems are essential for enabling the reduction of combusted iron back to iron, making them a critical component in the regeneration step of the cycle. This study investigates the impact of operating gas velocity on conversion by performing reduction experiments at three distinct fluidization numbers ( u s / u mf ): 16 (bubbling regime), 55 (transition region), and 100 (fully turbulent regime). Experiments were conducted to determine the appropriate velocities for each regime, ensuring optimal fluidization conditions across reduction temperatures ranging from 500 to 700 ∘ C. The results reveal that conversion rates increase significantly with gas velocities. At 500 ∘ C, operating at approximately six times higher velocity leads to a sixfold improvement in conversion when using iron-oxide particles with a Sauter mean diameter of 61 µm. However, while enhanced velocities improve reaction efficiency, challenges remain at elevated temperatures (T ≥ 500 ∘ C), where iron undergoes defluidization when exposed to hydrogen. Once defluidization occurs, refluidization proves impossible with either hydrogen or nitrogen, raising concerns about process stability. These insights highlight the potential for optimizing fluidized bed reduction through velocity control, while also underscoring the need for additional measures to mitigate unstable fluidization during high-temperature iron oxide reduction. • At 500 ∘ C, a conversion of 11 wt% is achieved after one hour of reduction in bubbly regime (fluidization number of 16). This increases to 66 wt% under identical conditions when operating in a turbulent regime (fluidization number of 100). • Particle agglomeration occurs in all experiments, becoming more pronounced at T > 500 ∘ C. • Defluidization at high temperature ( T ≥ 500 ∘ C) with iron is irreversible, as the bed remains defluidized once it occurs.

Institutions

Publication Details

Journal
Fuel
Published
2025-11-10
DOI
https://doi.org/10.1016/j.fuel.2025.137393
Citations
1
Primary Topic
Iron and Steelmaking Processes
Type
article
Field-Weighted Citation Impact
0.71
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Hydrogen reduction of combusted iron powder: Role of the fluidization regime on the conversion

1 citations
Fuel
Iron and Steelmaking Processes
0.71
article

Hydrogen reduction of combusted iron powder: Role of the fluidization regime on the conversion

article en
1 citations

Abstract

Fluidized bed systems play a crucial role in industrial processes such as combustion and gasification. In the Iron Power Cycle, fluidized bed systems are essential for enabling the reduction of combusted iron back to iron, making them a critical component in the regeneration step of the cycle. This study investigates the impact of operating gas velocity on conversion by performing reduction experiments at three distinct fluidization numbers ( u s / u mf ): 16 (bubbling regime), 55 (transition region), and 100 (fully turbulent regime). Experiments were conducted to determine the appropriate velocities for each regime, ensuring optimal fluidization conditions across reduction temperatures ranging from 500 to 700 ∘ C. The results reveal that conversion rates increase significantly with gas velocities. At 500 ∘ C, operating at approximately six times higher velocity leads to a sixfold improvement in conversion when using iron-oxide particles with a Sauter mean diameter of 61 µm. However, while enhanced velocities improve reaction efficiency, challenges remain at elevated temperatures (T ≥ 500 ∘ C), where iron undergoes defluidization when exposed to hydrogen. Once defluidization occurs, refluidization proves impossible with either hydrogen or nitrogen, raising concerns about process stability. These insights highlight the potential for optimizing fluidized bed reduction through velocity control, while also underscoring the need for additional measures to mitigate unstable fluidization during high-temperature iron oxide reduction. • At 500 ∘ C, a conversion of 11 wt% is achieved after one hour of reduction in bubbly regime (fluidization number of 16). This increases to 66 wt% under identical conditions when operating in a turbulent regime (fluidization number of 100). • Particle agglomeration occurs in all experiments, becoming more pronounced at T > 500 ∘ C. • Defluidization at high temperature ( T ≥ 500 ∘ C) with iron is irreversible, as the bed remains defluidized once it occurs.

FuelVol. 407
Eindhoven University of Technology (NL)
Openalex Percentile: Top 24%
Iron and Steelmaking Processes
0.71
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.