where C0 is the CO2 concentration in the gas mixture at the bed entrance, Ct is the CO2 concentration in the gaseous effluent stream at time t (min), xCO2 is the mole fraction of the CO2 in the gas mixture at the bed entrance, mi is the initial dry weight of the
adsorbent (kg), Q is the volumetric flow rate of the gas mixture at the bed entrance (L at STP/min), t0 is the time when the CO2 concentration in the gaseous effluent stream becomes above zero,tb is the time when the content of CO2 in the gaseous effluent stream reaches 2%, and ts is the time when the content of CO2 in the gaseous effluent stream reaches 40%.
where C0 is the CO2 concentration in the gas mixture at the bed entrance, Ct is the CO2 concentration in the gaseous effluent stream at time t (min), xCO2 is the mole fraction of the CO2 in the gas mixture at the bed entrance, mi is the initial dry weight of theadsorbent (kg), Q is the volumetric flow rate of the gas mixture at the bed entrance (L at STP/min), t0 is the time when the CO2 concentration in the gaseous effluent stream becomes above zero,tb is the time when the content of CO2 in the gaseous effluent stream reaches 2%, and ts is the time when the content of CO2 in the gaseous effluent stream reaches 40%.
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