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100 90 80 70 60 Recovery Purity 100 98 96 94 92 90 20 40 60 80 100 Temperature [°C] Figure 4.4 Effect of temperature on the CO2 purity and CO2 recovery in the heavy product. 4.2 MODEL PREDICTION OF THE PSA EXPERIMENTAL RESULTS In a previous study, the dynamic adsorption process simulator (DAPS) was validated against the experiments performed in the 1-bed PSA apparatus. The DAPS model was validated against the experimental data obtained in the five runs in single bed PSA apparatus described in previous study. This validated DAPS was used to predict the experimental results of the 4-bed PSA apparatus. The simulations was performed using the equilibrium and kinetic information of the 13X zeolite for the given gases independently in separate measurement methods. As explained before the equilibrium isotherm of both 28 CO2 Recovery [%] CO2 Purity [%]PDF Image | Development of a Pressure Swing Adsorption (PSA) Cycle for CO2 Capture
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