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TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION

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TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION ( temperature-swing-adsorption-processes-for-gas-separation )

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Figure 3.9. Water temperature at the microchannel outlet for the TSA cycle for the baseline case (100 kPa). Green region shows the 0.69 s for which the water exits the microchannel at 200°C, while cooling has already commenced near the microchannel inlet. Table 3.4. Heat recovery during cooling stage. ΔP 100 kPa 25 kPa 10 kPa Useful time for heat recovery [s] 0.69 1.10 2.21 Water mass flow rate [kg s-1] 20.1×10-4 13.2×10-4 7.07×10-5 Integrated heat recovered [MJ kg-ads-1] 8364 8682 9316 Energy savings with heat recovery [%] 14.6 28.7 33.9 88

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TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION

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