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in 0.3 s and the entire adsorbent layer is nearly regenerated in about 6 s. It should be noted that the maximum CO2 adsorbed concentration for all the cases is similar, which shows equal adsorbent layer utilization, regardless of the diameter. Figure 2.7. Effect of variation of microchannel diameter on (a) product purity and (b) CO2 adsorbed concentration for a constant adsorbent layer thickness of 30 μm. Table 2.5 shows the mass of product collected normalized with the adsorbent mass during the adsorption stage for the range of Dh considered. As the diameter increases, the product mass collected increases more sharply than the increase in the 45PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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