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Figure 4.15. SEM images of zeolite 5A adsorbent particles used for fabrication of custom-made adsorbent-coated microchannels Figure 4.16 shows model validation for the test results shown in Figure 4.13 for an assumed particle sizes of 7 μm (Figure 4.16(a) and (b)) and 2 μm (Figure 4.16(c) and (d)). The temperature rise trends are significantly affected with a change in adsorbent particle size. With a greater adsorbent particle size, the rate of adsorption into the adsorbent decreases in accordance with Equation (4.16). The rate of adsorption directly affects the rate of temperature rise as seen from the energy conservation equation for the adsorbent layer shown in Table 4. Therefore, for an adsorbent size of 7 μm, the rate of temperature increase is low (Figure 4.16(a).) Fluid flow within the microchannel is not affected with changes in adsorbent particles size; therefore, while the adsorption in the adsorbent layer continues at a lower rate, the feed gas wave front reaches the 142PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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