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Figure 3.8. (a) Effect of reduction in desorption temperature on operating adsorption swing capacity, seen as the difference between adsorption stage peak value near 1 s and lowest value after cooling stage at 7 s. (b) Effect of drop in temperature on product purity. The other major energy consumption of the cycle is by the purge gas compressor, and is more critical because it is in the form of electrical energy input. The baseline case imposes a 100 kPa pressure drop across the microchannel. This pressure drop can be reduced to decrease the compressor power by reducing not only the specific volume change, but also the mass flow rate through the compressor. The reduced pressure drop, however, decreases the mass flow rate though the microchannel for all the stages, and not just for the purge stage. Hence, all the stage times must be recalculated, as the times in Table 3.1 change depending on flowrates of the component mixture and the HTF through 84PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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