Evaluation of the Effects of Fluidization Conditions on Hydrogen Reduction in Manganese Ore Fines

Hydrogen prereduction of two manganese ores fines was investigated under varied operating conditions in a fluidized bed. The manganese ores used in this study are the Zambian ore and the South African Nchwaneng ore from the Kalahari region. The samples were milled and sized before they were characterized with regard to sphericity, Inductively Coupled Plasma Optical Emission Spectroscopy (ICP-OES) chemical analyses, X-ray diffraction (XRD) analyses and Scanning Electrons Microscope (SEM) analyses. Prereduction experiments were conducted in a laboratory scale fluidized bed with the parameters of interest being minimum fluidization velocity, terminal velocity, elutriation, average bed voidage, residence time, temperature, intrinsic ore properties and cohesive adhesion. Experiments for the determination of fluidization velocity and terminal velocity were conducted at both ambient temperature and elevated temperature (500 °C, 550 °C, 600 °C, 700 °C, 800 °C and 900 °C), and for varied sample masses (100 g, 300 g and 700 g) and varied particle-size ranges (200–300 μm, 300–425 μm, 425–500 μm and 500–600 μm). The experimentally observed minimum fluidization velocities for particles size groupings of [+106–200 μm], [+200–300 μm], [+300–425 μm], [+425–500 μm] and [+500–600 μm] as well as the mix (20 wt% of each) was comparable with the theoretical minimum fluidization velocity. The fluidized bed was heated to a desired temperature at a rate of 10 °C/min under argon whilst logging the pressure drop across the bed with increasing temperature. The convectional cooling during the introduction of cold hydrogen as well as the net energy of endothermic and exothermic chemical reactions were observed to result in a temperature drop in the order of 100 to 250 °C. Thermal mineral transformation under argon was observed to yield iron manganese oxide in the order of 15 to 30 wt/wt%. Prereduction was conducted using hydrogen gas at a desired temperature and terminal velocity. Reduction extent was observed to increase with the increasing temperature and residence time. Increasing reduction temperature beyond 700 °C was not observed to improve reduction, whereas longer residence time (of up to 40 min) was observed to favor the formation of iron manganese oxide, iron manganese and manganosite. For hydrogen prereduction experiment conducted at 900 °C, the reactor was observed to be brittle after the experiment. Cohesive adhesion was observed to be more pronounced at 900 °C.

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Publication Details

Journal
Minerals
Published
2025-04-01
DOI
https://doi.org/10.3390/min15040368
Citations
2
Primary Topic
Mineral Processing and Grinding
Type
article
Field-Weighted Citation Impact
1.43

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article

Evaluation of the Effects of Fluidization Conditions on Hydrogen Reduction in Manganese Ore Fines

Dursman Mchabe, Sello Tsebe, Elias Matinde
2 citations
Minerals
Mineral Processing and Grinding
1.43
article

Evaluation of the Effects of Fluidization Conditions on Hydrogen Reduction in Manganese Ore Fines

Dursman Mchabe, Sello Tsebe, Elias Matinde
article en
2 citations

Abstract

Hydrogen prereduction of two manganese ores fines was investigated under varied operating conditions in a fluidized bed. The manganese ores used in this study are the Zambian ore and the South African Nchwaneng ore from the Kalahari region. The samples were milled and sized before they were characterized with regard to sphericity, Inductively Coupled Plasma Optical Emission Spectroscopy (ICP-OES) chemical analyses, X-ray diffraction (XRD) analyses and Scanning Electrons Microscope (SEM) analyses. Prereduction experiments were conducted in a laboratory scale fluidized bed with the parameters of interest being minimum fluidization velocity, terminal velocity, elutriation, average bed voidage, residence time, temperature, intrinsic ore properties and cohesive adhesion. Experiments for the determination of fluidization velocity and terminal velocity were conducted at both ambient temperature and elevated temperature (500 °C, 550 °C, 600 °C, 700 °C, 800 °C and 900 °C), and for varied sample masses (100 g, 300 g and 700 g) and varied particle-size ranges (200–300 μm, 300–425 μm, 425–500 μm and 500–600 μm). The experimentally observed minimum fluidization velocities for particles size groupings of [+106–200 μm], [+200–300 μm], [+300–425 μm], [+425–500 μm] and [+500–600 μm] as well as the mix (20 wt% of each) was comparable with the theoretical minimum fluidization velocity. The fluidized bed was heated to a desired temperature at a rate of 10 °C/min under argon whilst logging the pressure drop across the bed with increasing temperature. The convectional cooling during the introduction of cold hydrogen as well as the net energy of endothermic and exothermic chemical reactions were observed to result in a temperature drop in the order of 100 to 250 °C. Thermal mineral transformation under argon was observed to yield iron manganese oxide in the order of 15 to 30 wt/wt%. Prereduction was conducted using hydrogen gas at a desired temperature and terminal velocity. Reduction extent was observed to increase with the increasing temperature and residence time. Increasing reduction temperature beyond 700 °C was not observed to improve reduction, whereas longer residence time (of up to 40 min) was observed to favor the formation of iron manganese oxide, iron manganese and manganosite. For hydrogen prereduction experiment conducted at 900 °C, the reactor was observed to be brittle after the experiment. Cohesive adhesion was observed to be more pronounced at 900 °C.

MineralsVol. 15(4)
Mintek (ZA)
Mintek, European Commission, HORIZON EUROPE Framework Programme
Openalex Percentile: Top 21%
Mineral Processing and Grinding
1.43
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