Chemical Engineering & Technology · 2011 · 99 citations · 10 references
EngineeringChemical EngineeringChemistryGreen ChemistryReaction EngineeringResource RecoveryCarbon Dioxide RemovalSolvent ExtractionEnergy ConsumptionExergyExtraction SolventsSolvent RegenerationTemperature Effects On ExtractionWaste Heat RecoveryWaste Heat Utilization
The key challenge in amine-based CO2 capture from flue gases is to reduce the energy consumption required for solvent regeneration. Lipophilic amines exhibit a thermomorphic phase transition upon heating, giving rise to autoextractive behavior, which intensifies desorption at temperatures well below the boiling point of aqueous solutions. The low regeneration temperature of less than 80 °C together with the high cyclic CO2 loading capacity of ∼0.9 mol molabsorbent–1 of such thermomorphic biphasic solvent (TBS) systems permit the use of low-value and even waste heat at temperatures below 100 °C for desorption. In order to reduce the exergy demands still further, techniques for enhancing CO2 release using extractive regeneration with inert solvent addition were investigated at temperatures of 40–50 °C to permit the use of waste heat at temperatures of ∼70 °C or less. The regeneration of 3 M absorbed lipophilic amine solutions with 0.93 mol mol–1 CO2 loading by using various additional solvents and the evaluation of the extractive performance in multiple-stage crosscurrent and countercurrent configurations indicated the promise of adding certain hydrophobic solvents to enhance the low-temperature regeneration of TBS absorbents.
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Amine Scrubbing for CO <sub>2</sub> Capture
Gary T. Rochelle · Science · 2009 · 4.3K citations
Engineering, Chemical Engineering, Environmental Engineering +14
Synthesis and selection of hindered new amine absorbents for CO2 capture
Firoz Alam Chowdhury, Hiromichi Okabe, Hidetaka Yamada et al. · Energy Procedia · 2011 · 168 citations · Full text