Abstract
An energy efficient proprietary mixed solvent for the separation of CO2 from power plant flue gas streams has been developed. The solvent combines the higher reaction rate of a more reactive solvent and the lower heat of reaction of a less reactive solvent and achieves mass transfer rates similar to more reactive monoethanolamine (MEA) solvent via a catalytic mechanism. The regeneration energy required is 30% less than conventional MEA. Solvent losses and corrosion rates are 10 and 5 times lower than MEA, respectively. © 1995.
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CITATION STYLE
Chakma, A. (1995). An energy efficient mixed solvent for the separation of CO2. Energy Conversion and Management, 36(6–9), 427–430. https://doi.org/10.1016/0196-8904(95)00036-D
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