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Comparison with Absorption and Membrane Technology

The economics of the CPB concept is compared to absorption and membrane technology in this section. In order to present a comparison as fair as possible, costs are calculated based on the same cost parameters as that used in the evaluation of the cryogenic concept. [Pg.45]

The required input for the evaluation of CO2 capture costs via absorption technology is obtained from the Integrated Environmental Control Model developed by Rubin [23]. A 600 MW power plant with monoethanolamine (MEA) absorption was simulated, resulting in a flue gas of 666 kg/s containing 14 vol% CO2 (on a dry basis), which is similar to the flue gas composition that used in the evaluation of the cryogenic concept. The costs for all [Pg.45]

Amine scrubbing Equipment Module costs (M ) Membrane Equipment Module costs (M ) [Pg.46]

Total direct investment 299.3 Total direct investment 500 [Pg.46]

Total allocated investment 119.7 Total allocated investment 200 [Pg.46]


Tuinier MJ, Hamers HP, van Sint Annaland M (2011) Techno-economic evaluation of cryogenic CO2 capture a comparison with absorption and membrane technology. Int J Greenhouse Gas Control 5 1559-1565... [Pg.218]


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