Abstract
Optimization of integrated carbon capture processes is considered essential for addressing the challenges of low capture efficiency and high costs associated with low-concentration CO2 streams, thereby advancing low-carbon industrial practices. In this context, an adsorption-coupled cryogenic liquefaction process is proposed. Process efficiency and system energy consumption under diverse feed conditions were systematically evaluated via simulation. Techno-economic assessment was performed considering the trade-off between capture performance and energy requirements. Simulation results indicate that at feed CO2 concentrations of 5–15%, capture rates of 80.60–81.50% were achieved with product purity of 98.60–98.94%, while energy consumption ranged from 4.012 to 4.494 GJ/tCO2. When optimizing for a 90% capture rate, product purity increased by 0.1% on average, though a 7.34% average increase in energy consumption was observed. Integration of this process with recoverable cold energy from gas-fired power plants could reduce energy consumption by >2 GJ/tCO2, significantly lowering operational demands. This approach provides a validated pathway toward decarbonizing industrial systems, demonstrating both theoretical and practical significance for achieving carbon neutrality.
Keywords Carbon capture, Process optimization, adsorption, cryogenic liquefaction process
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Energy Proceedings