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: The study presents an analysis of a hybrid CO 2 capture system integrating a combined cycle gas turbine (CCGT) with two separation technologies: amine-based CO 2 capture from flue gas (CCS) and membrane direct air capture (m-DAC). The novelty lies in combining both methods in a single system to reduce energy intensity and increase operational flexibility. Different operating configurations were analyzed, including the flue gas split between the amine and membrane units and the ratio of air supplied to the m-DAC unit relative to the flue gas stream ( ). The best results were obtained when the entire flue gas stream was directed to the absorption column ( ) and the cleaned gas was mixed with air and supplied to the m-DAC module. This increased the CO 2 concentration at the m-DAC inlet, with energy intensity ranging from 1.70 to 9.03 GJ/t CO 2 and captured CO 2 flow from 4819 kg/h to 5742kg/h, depending on . The ratio also determines the system’s mode of operation: at low values, it functions as a classical CCS unit improving CCGT emissions, while at high values, it operates as a direct air capture unit. The CO 2 recovery rate ( ), calculated relative to CO 2 produced from methane combustion in the CCGT, exceeded 100% in all scenarios, indicating a net-negative CO 2 balance within the plant boundary. The system allows for high-purity CO 2 capture: >95% for the amine unit and >85% for the m-DAC module. The results confirm that hybrid CCS/DAC systems represent an energy-efficient and flexible solution for future CO 2 capture technologies.
Niesporek et al. (Mon,) studied this question.
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