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whether PSA, VSA or TSA, and the shape depends on the results obtained for a range of impurities up to 1% of SO2, NO2 and H2O in the inlet flue gas (see also Figure 5). It can be seen that recovery increases monotonically with purity in all three structures as the impurity content is increased, to a point where purity reaches its limit and shows a sharp drop in its value (or increase in some cases). The sudden change in that point is governed by the amount of carbon dioxide and the amount of nitrogen and impurities contained in the adsorption bed: a reduction in the CO2 working capacity due to the uptake of competing components yields lower purities, while negligible N2 working capacities allow higher purities. 100% 90% 80% 70% 60% 50% 40% 30% 20% 10% 0% 0% 100% 90% 80% 70% 60% 50% 40% 30% 20% 10% 0% 0% 20% 40% Recovery 80% 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 100% 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 100% no imp. 1% imp. no imp. 20% 40% Recovery 35 80% 60% 60% 1% imp. Purity PurityPDF Image | swing adsorption processes for CO2 capture in selected MOFs and zeolites
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