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C.1 Instantaneous heat and mass transfer resistance calculation For this section, an instant during displacement of gas by liquid is chosen, for a comprehensive demonstration of the modeling methodology. Calculations could also be shown at other instants, when a single phase occupies the entire length of the microchannel. The selected instant is 0.392 s, after the process is initialized and an adsorption stage of 0.19 s long is already completed. The calculation point under consideration is 0.5 m from both the ends of the microchannel. The displacing hot water has occupied the upstream node. At the current instant, gas-phase residual gases have occupied the node. At the following instant at 0.397 s, the displacing hot liquid occupies the same node. Figure C.2 shows the initial and final instants considered for the present sample calculation. The node at 0.5 m is shown to be occupied by component gases before the displacement of gas takes place and liquid occupies the same node. Figure C.2. Initial and final states of the displacement of gas used for the sample calculation. 180PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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