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cases, these times and the hot HTF mass flow rates and corresponding heat recovery calculations are shown in Table 3.4. Considering the component-wise energy requirements shown in Figure 3.6, the energy recovered during the cooling stage is significant (14.6% of the original value for the baseline case with 100 kPa without heat recovery from the cooling stage) and decreases the energy ratio to 12% from 14%. The lower pressure drop cases show more gains, because the total energy required has already decreased by nearly 52% of the energy requirement for the baseline case. The energy ratio calculations are repeated for the revised stage times and pressure drops, and the results are plotted in Figure 3.10, which shows reduced energy consumption over the baseline case, shown in Figure 3.7. It can be seen that the energy ratio falls to 5.7% and 6.1% for the 25 kPa and 10 kPa pressure drop cases, respectively as compared to 14% for the 100 kPa pressure drop case, with a sensible heat fraction of 96.2%. This means that the high-grade electricity requirement is only 3.8% of the total operating cost, while the source for the rest of the energy need not be electricity. 87PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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