(10c) Low CO2 Concentration Post-Combustion Capture: Process Insights | AIChE

(10c) Low CO2 Concentration Post-Combustion Capture: Process Insights

Authors 

Frimpong, R. - Presenter, University of Kentucky
Irvin, B., University of Kentucky
Nikolic, H., University of Kentucky
Liu, K., University of Kentucky
For post-combustion CO2 technologies applicable to power-plants, amine-based solvent CO2 capture has seen considerable development for commercial deployment among other available options. Although amine-based solvent CO2 capture has been in use for several decades in gas sweetening applications for example, a key technological challenge for post-combustion CO2 capture in fossil-fuel power generating plants is the low CO2 concentration in the flue gas. Typical concentrations range from 12-14 vol% for coal-fired plants and 3-5 vol% for natural-gas fired plants. The low concentration reduces the driving force for CO2 transfer from the gas phase into the solvent with its consequent impact on the energy of regeneration of the solvent. With technology suited to both natural and coal-fired gas plants, the even lower drying force for CO2 transfer from natural gas generated-flue gas would require stringent process conditions to overcome the effect of this limitation such as the potentially higher energy implications for solvent regeneration, with the associated high cost of electricity.

In this work, results from experiments conducted in a 0.1 MWth pilot post-combustion CO2 capture unit at low CO2 concentration (~5 vol%) mimicking natural gas-fired plant conditions is presented. Impacts of different liquid circulation, gas flow rate and stripper pressure were examined. The results of the study was compared with findings from studies done with coal-derived flue gas. It is shown that appropriate hydrodynamic conditions in the column are required for the low CO2 concentration based on reduced liquid circulation rates to enhance solvent performance as a result of the low driving force for capture. The corresponding higher oxygen content in the low-content CO2 gas did not contribute to increased oxidative solvent degradation compared to the impact of the stripping temperature. Leveraging extensive work done with high CO2 flue gas conditions (applicable to coal-fired plants), comparisons will highlight applicability of knowledge to natural-gas fired plants together with recommended areas for process enhancement, particularly as these plants increase in prominence for power generation.

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