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Figure 3.3. Schematic showing limits of product recovery from the purification process. Figure 3.3(a) shows the adsorption stage scenario resulting in the least possible product collection from the process. If the feed gas supply continues for a small duration after the start of the adsorption stage, and both the inlet and outlet gas valves are turned off simultaneously afterwards, no feed gas can enter the product resulting in negligible net product collection. In contrast, Figure 3.3(b) shows the case when product collection is the highest. This is possible as a result of continued product collection until the liquid- gas interface reaches the microchannel outlet, even after the feed supply is cut off. Depending on the selection of feed times and product collection times in between the two extremes shown in Figure 3.3(a) and Figure 3.3(b), a performance matrix can be generated. The purity calculation in the product tank is shown in Equations (2.25) through (2.27), while CH4 recovery is calculated as shown in Equation (3.9). 75PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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