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TEMPERATURE SWING ADSORPTION COMPRESSION AND MEMBRANE SEPARATIONS

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TEMPERATURE SWING ADSORPTION COMPRESSION AND MEMBRANE SEPARATIONS ( temperature-swing-adsorption-compression-and-membrane-separa )

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440 430 420 410 400 390 380 370 50 60 70 80 90 100 Percent of total energy supplied by one heater (%) Adsorption, k=100 W/m K Adsorption, k=0.135 W/m K Adsorption, k=0.27 W/m K Adsorption, 2xL Figure 3.7: Mass of CO2 in the adsorbed phase per unit depth of the adsorbent bed after an adsorption half-cycle for a realistic, large, and doubled value of thermal conductivity. The curve labeled 2×L used k = 0.135 W/m K and has half the height and twice the length of the other geometry (i.e., Y has been halved and L has been doubled) with the heaters modified proportionately.. 40 Mass of CO2 in adsorbed phase (g/m)

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