M. Baniam, Z. Mohammadi, E. Gholamian, A. Saberi Mehr
The integration of carbon capture, utilization, and storage (CCUS) into energy systems is a key pathway toward low-carbon energy transition, yet most existing studies treat CO₂ capture and utilization as auxiliary processes and assess system performance under fixed operating conditions. In this study, a fully integrated CCUS-enabled polygeneration system is developed and evaluated to simultaneously produce electricity, hydrogen, and synthetic natural gas (NG) within a closed-loop framework. The proposed configuration integrates a renewable-powered proton exchange membrane electrolyzer, an anaerobic digestion unit for biomass-derived carbon supply, a solid oxide fuel cell (SOFC) for high-efficiency power generation, and multi-stage membrane separation trains for selective hydrogen purification and CO₂ recovery. A comprehensive parametric and scenario-based analysis is conducted to quantify the coupled effects of membrane stage-cut distributions, SOFC current density and inlet temperature, and the fraction of captured CO₂ routed to fuel synthesis. The membrane separation trains achieve hydrogen and CO₂ purities exceeding 99.9% and 95%, respectively, while maintaining acceptable pressure drops. Across eight operating scenarios, the overall energy efficiency varies between approximately 0.30 and 0.46, with total product unit costs ranging from about 33.01–114.5 $/GJ. The lowest specific CO₂ emissions and highest system efficiency are obtained under moderate SOFC current density and optimized membrane operation, whereas maximum net power output is achieved under low pressure-drop conditions. The results identify clear trade-offs among power generation, hydrogen storage, economic performance, and carbon emissions, providing practical design guidelines for optimizing integrated CCUS-based energy systems under realistic operating conditions. • CCUS hub co-produces electricity, H₂, SNG from biogenic CO₂ and wind power. • Membrane trains achieve 99.9% H₂ and 95% CO₂ purities with acceptable pressure drops. • Eight scenarios based on SOFC working conditions and permeator states are analyzed. • System obtains near-zero emissions of 0.001328 kg CO₂/kWh via biogenic CO₂ recycling. • Optimal CO₂ allocation to the SNG unit (0.1–0.4) minimizes both cost and emissions.