Adsorption processes for CO2 separation can be heavily impacted by feed gas humidity, especially when hydrophilic adsorbents such as zeolite 13X are used. In this work, a hydrophobic ZSM-5 zeolite is studied for CO2 separation from postcombustion flue gas (CO2/N2) and off-gas from electrochemical CO2 capture and conversion processes (CO2/O2) without extensive feed gas drying. The binary CO2/H2O equilibrium was probed, demonstrating that more than 90% of the CO2 adsorption capacity of zeolite 13X is lost under humid conditions, whereas ZSM-5 zeolite retains 83% of its CO2 adsorption capacity at a relative humidity up to 62%. The ternary CO2/N2/H2O and CO2/O2/H2O equilibria were modeled and pressure-vacuum swing adsorption (PVSA) processes for CO2 separation from humid flue gases and electrolysis gases were optimized. Purity ≥ 95% and recovery ≥ 90% can be achieved for both feed gases under high humidity conditions using ZSM-5 zeolite. For CO2 separation from electrolysis gases, with a higher CO2 content, purity-recovery requirements can be met in PVSA processes operating at mild vacuum pressure (100 mbar) with an energy consumption down to 0.084 kWh/kg CO2.
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Born et al. (2026) studied this question.
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