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The electrical input required for recirculation of the HTF is calculated using Equation (3.12). After separating the mixture components in gaseous form in the desorption sink, the HTF, which also carries dissolved component gases, is recirculated to the monolith inlet neglecting losses from the pipelines. EHTF,recir NcycNch MHTF,cyc vHTF P (3.12) Finally, the compressor input power required to recirculate the purge gas from the product gas tank to the monolith inlet for the entire duration of the purge stage is calculated as shown in Equation (3.13) (assuming isentropic compression.) E purge N cyc Nch HCom (3.13) For the standard operating case with the stage times shown in Table 3.1, the predicted energy requirements for each of the components are shown in Figure 3.6. It can be seen that the heat of desorption is only 10.3 % of the sensible heat requirement, while the sensible heat itself is about 42% of the total energy required. Figure 3.6. Component-wise energy requirement for the baseline case. 80PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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