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By Nicolás A Mazzeo

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Example text

E. lower) the emission of these air pollutants directly and indirectly. The consumption of solvent in the capture process is an important driver for solvent development as solvent loss deteriorates operational economics and has environmental consequences. The consumption of the solvent varies per type of solvent but is for postcombustion typically in the order of 1-2 kg/tonne CO2 captured. 3 kg/tonne captured (Moser et al. 2011). Typically, the consumption of MEA is higher compared to its alternatives.

In the following compression & purification step additionally NOx, SOx, HCl, water and heavy metals are removed as condensate from the compressors, and with the use of an activated carbon filter and an adsorber (Burchhardt 2009;Thébault, Yan et al. 2009;Yan, Faber et al. 2009). Overall, a deep reduction of SO2 and NOx emissions is expected to be possible with oxyfuel combustion, although R&D is required to better understand the behaviour of these substances in the CO2 compression & purification process.

The typically higher conversion efficiency for gasification or reforming results however in typically lower net CO2 emissions for the pre-combustion concepts (21-97 g/kWh) compared to the postcombustion concepts (55-143 g/kWh). 2 Sulphur dioxide In the coal fired power plants equipped with post-combustion CO2 capture, SO2 emissions are reduced significantly compared to a power plant without capture. One reason is that power plants with CO2 capture should be equipped with improved flue gas desulphurization (FGD) facilities (Tzimas, Mercier et al.

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