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Figure 4.7. (a) Heat transfer resistance networks from microchannel gas node to the ambient temperature node (b) Dimensions of the thermal mass nodes. The mass transfer resistance calculated in Equation (4.10) and the heat transfer resistances calculated using Equations (4.20) through (4.22) are substituted in the total mass, species, momentum and energy conservation equations for the adsorbent-coated microchannel nodes, adsorbent layer nodes, and fused silica cover nodes and are coupled with each other, as shown in Table 4.4. This coupling helps in predicting the fused silica coating temperature, which can be compared with the measured temperatures. The axial dispersion coefficient, DA,i, in the species balance equation for the microchannel is calculated as shown in Equation (4.28) (Cussler, 1997). The boundary conditions and initial conditions for the governing equations are also listed in Table 4.4. The conservation equations for the adsorbent-coated microchannel assembly are coupled with the inlet and outlet headers as shown in Figure 4.5. Pei uDh DAB ,i (4.28) D D 1Pe2 A,i AB,i i 192 125PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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