Multi-objective optimization of a hybrid carbon capture plant combining a Vacuum Pressure Swing Adsorption (VPSA) process with a Carbon Purification unit (CPU).

• Study of hybrid CO 2 capture system combining VPSA and CPU technologies. • Optimization of integrated capture CO 2 process and purification unit. • High CO 2 recovery (90–99 %) and high CO 2 purity (>99.99 %) • Complete analyses considering recovery, energy consumption, and capture cost. • Impact of the electricity source on the total CO 2 recovery. The imperative challenge posed by climate change requires urgent actions to counteract the harmful effects of greenhouse gas emissions, particularly CO 2 , which contributes to approximately 80 % of emissions responsible for global warming. A hybrid system combining Vacuum Pressure Swing Adsorption (VPSA) unit with a Cryogenic Carbon Purification Unit (CPU) is evaluated to enhance recovery and purity of CO 2 captured from flue gas containing CO 2 concentration ranging from 5 % to 20 %. VPSA preconcentrates the CO 2 and CPU completes the separation and purifies the CO 2. The study uses surrogate models for multi-objective optimization, considering energy consumption, cost, and CO 2 recovery, providing a time-efficient approach for investigating computationally demanding processes. Results from the study indicate that the hybrid system achieves over 90 % recovery for flue gas concentration range considered, while ensuring the production of high-purity CO 2 (>99.99 %) suitable for transportation. A trade-off analysis reveals the balance between recovery, electricity consumption, and economic viability. A sensitivity analysis identifies parameters influencing recovery and energy consumption, providing guidance for future optimization efforts. The techno-economic analysis highlights the impact of electricity prices and carbon taxes on total costs, identifying an optimum towards higher recovery values under rising carbon taxes. Furthermore, the research underscores concentration-dependent economic feasibility, emphasizing the attractiveness of concentrations above 10 % compared with other technologies, which require higher concentrations. For an electricity price of 75 €.MWh−1, the total cost of the CO 2 capture hydride system considering CO 2 emissions with carbon tax of 100 €.t CO2 −1 for concentrations ranging from 10 % to 20 % is from 123 to 80 €.t CO2 −1, respectively. The analysis of the electricity source shows the importance of a low-carbon emission energy mix for optimal carbon emission reduction. [ABSTRACT FROM AUTHOR]