Optimizing rotary kiln operations for molybdenite concentrate oxidation roasting to produce molybdic trioxide

• Understanding the MoS 2 – MoO 2 – MoO 3 relationship and its equilibrium is important. • The MoO 3 conversion of 97–98 % was obtained at 5–10 rpm and 550–600 °C. • Agglomeration is more pronounced without drum rotation and at higher temperatures. • Optimal MoO 3 production requires appropriate drum rotational speeds and temperatures. The effects of the rotational speed (0–10 rpm) and temperature (550–650 °C) of rotary kiln drums on the oxidation roasting of molybdenite (MoS 2 ) concentrate was investigated in this study. Computational predictions indicated that production of MoO 2 was more favorable than that of MoO 3 up to a certain stage of the oxidation roasting process, after which MoO 3 is produced through the consumption of MoO 2 . Thus, understanding the MoS 2 –MoO 2 –MoO 3 relationship and its equilibrium is important. A drum rotational speed > 5 rpm significantly increased the S reduction rate and considerably decreased the S content at 60 min to < approx. 5 %. Additionally, the S content at 60 min decreased with decreasing the temperature from 650 to 550 °C due to the MoS 2 concentrate exothermic reaction during oxidation roasting. The MoS 2 to Mo x O y (≈ MoO 2 +MoO 3 ) conversion rate (%) was generally proportional to the rotational speed and reaction duration. X-ray diffraction analysis indicated that 5–10 rpm and 550–600 °C yielded a higher experimental conversion rate (97–98 %). Furthermore, the MoO 2 and MoO 3 conversions were separately quantified. Agglomeration was more pronounced without drum rotation and at higher temperatures. Analysis of the reaction kinetics using the unreacted-core model indicated that diffusion through the gas film layer is supported by the 20.9 kJ/mol activation energy obtained from the Arrhenius plot. Consequently, an appropriate drum rotational speed at a relatively low temperature is a prerequisite for producing MoO 3 through the oxidation roasting of MoS 2 concentrates in a rotary kiln.

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Publication Details

Journal
Chemical Engineering Journal Advances
Published
2024-08-26
DOI
https://doi.org/10.1016/j.ceja.2024.100642
Citations
3
Primary Topic
Iron and Steelmaking Processes
Type
article
Field-Weighted Citation Impact
0.64

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article

Optimizing rotary kiln operations for molybdenite concentrate oxidation roasting to produce molybdic trioxide

Seongsoo Han, Youngjae Kim, Jung Ho Heo, Hyun Sik Park et al.
3 citations
Chemical Engineering Journal Advances
Iron and Steelmaking Processes
0.64
article

Optimizing rotary kiln operations for molybdenite concentrate oxidation roasting to produce molybdic trioxide

Seongsoo Han, Youngjae Kim, Jung Ho Heo, Hyun Sik Park, Seunghyeon Baek, Kurniawan Kurniawan, Joobeom Seo
article en
3 citations

Abstract

• Understanding the MoS 2 – MoO 2 – MoO 3 relationship and its equilibrium is important. • The MoO 3 conversion of 97–98 % was obtained at 5–10 rpm and 550–600 °C. • Agglomeration is more pronounced without drum rotation and at higher temperatures. • Optimal MoO 3 production requires appropriate drum rotational speeds and temperatures. The effects of the rotational speed (0–10 rpm) and temperature (550–650 °C) of rotary kiln drums on the oxidation roasting of molybdenite (MoS 2 ) concentrate was investigated in this study. Computational predictions indicated that production of MoO 2 was more favorable than that of MoO 3 up to a certain stage of the oxidation roasting process, after which MoO 3 is produced through the consumption of MoO 2 . Thus, understanding the MoS 2 –MoO 2 –MoO 3 relationship and its equilibrium is important. A drum rotational speed > 5 rpm significantly increased the S reduction rate and considerably decreased the S content at 60 min to < approx. 5 %. Additionally, the S content at 60 min decreased with decreasing the temperature from 650 to 550 °C due to the MoS 2 concentrate exothermic reaction during oxidation roasting. The MoS 2 to Mo x O y (≈ MoO 2 +MoO 3 ) conversion rate (%) was generally proportional to the rotational speed and reaction duration. X-ray diffraction analysis indicated that 5–10 rpm and 550–600 °C yielded a higher experimental conversion rate (97–98 %). Furthermore, the MoO 2 and MoO 3 conversions were separately quantified. Agglomeration was more pronounced without drum rotation and at higher temperatures. Analysis of the reaction kinetics using the unreacted-core model indicated that diffusion through the gas film layer is supported by the 20.9 kJ/mol activation energy obtained from the Arrhenius plot. Consequently, an appropriate drum rotational speed at a relatively low temperature is a prerequisite for producing MoO 3 through the oxidation roasting of MoS 2 concentrates in a rotary kiln.

Chemical Engineering Journal AdvancesVol. 20
Colorado School of Mines (US), Inha University (KR), Korea Institute of Geoscience and Mineral Resources (KR), Korea University of Science and Technology (KR)
Ministry of Trade, Industry and Energy, Korea Institute of Energy Technology Evaluation and Planning
Openalex Percentile: Top 36%
Iron and Steelmaking Processes
0.64
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