CO to compression
Flue gas to stack
Condenser
Lean amine
Condensate
Rich amine
Solvent regeneration column
CO absorption column
Steam
Flue gas 3 - 5 vol% CO
Rich amine
Reboiler
Condensate
Lean amine
Figure 1 Typical configuration of an amine-based carbon dioxide scrubbing system
the necessary heating for the desorption of the CO 2 . Reboiler bottoms are recycled back into the absorber, which provides regenerated lean amine ready to repeat the process. Amine scrubbers have a high CO 2 uptake capacity and relatively low initial capital
investment. However, they do suffer from some limitations. Firstly, the operational cost of amine scrubbers is expensive, mainly driven by the energy required to regenerate the amine once it is saturated with CO 2 . Amines absorb CO 2 through a strong chemical reaction, forming very stable bonds that require significant energy to break during regeneration. Our customers in the power generation space have pointed to energy penalties in the 30-40% range, representing a significant drop in productivity regarding both Capex and Opex. Due to the high energy input required, the reboilers are often large, further resulting in operational footprint restrictions. High-duty amine scrubbers have large space requirements, limiting their utility for smaller, more modular carbon capture duties. Lastly, certain amines present challenges from a material handling perspective. Most amines undergo oxidative degradation and thermally degrade at solvent regeneration temperatures above 120°C (Vega et al., 2014). It is estimated that this degradation leads to an average monthly replacement requirement of 5% of the amine. Amines also tend to corrode the process equipment and pipework, leading to higher overall Capex and maintenance-driven downtime. Metal-organic frameworks (MOFs) Initially discovered in 1965 as waste material from other chemical processes, MOFs are a
Figure 2 Simplified and modelled 3D representations of MOF structures comprising metal clusters and organic ligands (linkers)
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