Cited by 31CO2 Sequestration and Geologic InteractionsCarbon Dioxide Capture TechnologiesMagnesium Oxide Properties and Applications

Recent developments in the carbonation of serpentinite derived Mg(OH)2 using a pressurized fluidized bed

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Fagerlund, Johan, Nduagu, Experience, Zevenhoven, Ron·2011·Energy Procedia

Abstract

By using a pressurized fluidized bed (PFB) reactor for the carbonation of serpentinite derived Mg(OH)2 we want to utilize, for the purpose of minimizing process energy requirements, the exothermic reaction that leads to the binding of CO2 in a stable and environmentally benign form, MgCO3. Recent results show that most of the carbonation takes place only minutes into the experiment, suggesting that a carbonate layer forms on top of the Mg(OH)2 core and inhibits further carbonation. However, this problem might be eliminated/reduced by increasing the fluidization velocity. On the other hand, the suddenly lowered reactivity might also be the result of MgO formation, which is much less reactive than the initial Mg(OH)2. These and other aspects of gas/solid carbonation using a PFB being investigated include CO2 pressure, temperature, particle size, particle amount (or bed size) and water injection. The influence of temperature and pressure on the carbonation of Mg(OH)2 is evident, but the other factors are less clear. For instance, water has been shown by others to catalyze magnesium carbonation, but our results obtained so far using small amounts (0.1–2% vol- H2O/vol- CO2) of H2O injected into the CO2 stream have not confirmed this. This does not mean that H2O injection could not be beneficial, but implies that its effect has hitherto been clouded by other factors. Most of the experiments have been performed using commercially produced (Dead Sea Periclase Ltd.) Mg(OH)2, but progress in our Mg extraction process for magnesium silicate rock has resulted in sufficient amounts of Mg(OH)2 for use in our PFB reactor as well. Preliminary tests have been promising resulting in around 50% magnesium carbonation conversion in less than 10 minutes for Mg(OH)2 particles of 250–425 μm at 500 °C and 20 bar. In comparison, the Dead Sea Mg(OH)2 particles of same size fraction resulted in only 27% conversion in otherwise similar conditions. This is apparently a result of much lower porosity (0.024 vs. 0.24 cm3/g) and specific surface area (5.4 vs. 46.9 m2/g) for the Dead Sea Periclase sample.

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Crossref · 10.1016/j.egypro.2011.02.470

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  • Chemicals make up and intensive chemical regeneration hindered the deployment of the Maroto-Valer process.

    “However, chemicals make up and intensive chemical regeneration hindered the deployment of this process.”
  • Maroto-Valer et al. achieved a conversion of 55% in 10 minutes under mild conditions (20 1C and 40 bar) for carbonation of Mg(OH)2.

    “A conversion of 55% was achieved in 10 minutes under these mild conditions.”

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Authors
Fagerlund, J., Nduagu, E., & Zevenhoven, R.
Affiliations
Åbo Akademi University (FI)
Corresponding author
Zevenhoven, Ron
Venue
Energy Procedia
Publisher
Elsevier BV
Published
2011
Volume
4
Pages
4993-5000
ISSN
1876-6102 (ISSN-L)
OpenAlex
W2037698049
Cited by
31
References
4
Citations by year
2025: 1 · 2024: 3 · 2023: 3 · 2020: 1 · 2019: 2 · 2018: 2 · 2016: 3 · 2015: 4 · 2014: 3 · 2013: 3 · 2012: 2
FWCI
9.49
Type
conference paper
Language
en
Open access
Locations
  • Energy Procedia (publishedVersion, cc-by-nc-nd)
  • Åbo Akademi University Research Portal (publishedVersion, other-oa)
Topics
  • Physical Sciences › Environmental Science › Environmental Engineering › CO2 Sequestration and Geologic Interactions
  • Physical Sciences › Engineering › Mechanical Engineering › Carbon Dioxide Capture Technologies
  • Physical Sciences › Materials Science › Materials Chemistry › Magnesium Oxide Properties and Applications
Keywords
serpentinite, magnesium carbonate, CO2 sequestration, magnesium oxide formation, particle size effects

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