Abstract
A thermodynamic efficiency analysis using the exergy concept is used to assess CO 2 mineral sequestration process routes where electrochemical steps (electrolysis and fuel cells) are used to produce aqueous hydrochloric acid and sodium hydroxide reactant solutions. Results from three recent publications on the subject that come to different conclusions are used for this case study. It is shown that including electrolysis as one of the steps of a magnesium silicate mineral carbonation process route results in input energy requirements that will exceed the output of a fossil fuel-fired power plant that produces the CO 2 that is bound to (hydro-) carbonates. At the same time, fuel cells are not efficient enough to change this.
| Original language | English |
|---|---|
| Pages (from-to) | 1467-1472 |
| Number of pages | 6 |
| Journal | Chemical Engineering Research and Design |
| Volume | 90 |
| Issue number | 10 |
| DOIs | |
| Publication status | Published - Oct 2012 |
| MoE publication type | A1 Journal article-refereed |
Funding
This work is funded by the Academy of Finland's Sustainable Energy program (2008–2011), project Carbonates in Energy Technology (CarETech).
Keywords
- CO sequestration
- Electrolysis
- Energy efficiency
- Exergy
- Magnesium silicates
- Mineral carbonation
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