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The species conservation equation derived in Chapter 2 is modified to account for the absorbed fraction of gases in the HTF liquid. The rate of change of absorbed gas concentration in the HTF, derived in Equation (3.2), and the rate of change of gas concentration that is not absorbed and remains suspended in the HTF, constitute the overall species balance for the microchannel node. After this modification, the governing species balance equation used for microchannel flow is shown in Equation (3.5). C C uC S S X S X S D 2C g,i g,i,abs g,i ads LDG G GDL G Purge A,G,i g,i t t z SXSSSXD z Figure 3.1. Component architecture considered for modeling the TSA-based purification process. Also shown are the recirculation loops for purge gas and HTF. Sads SLDG XG SGDL XG SPurge 1 Req,Mass,G,i Cg,i Cw,i SLDG XL Sdeso Scool SGDL XL 1 Ag Req,Mass,L,i 0 LDG L deso cool GDL L A,L,i 2 (3.5) 71PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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