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5.1 Diagram of the experimental apparatus for removing water vapor using a Nafion⃝R membrane with a vacuum on the shell side which uses two relative humidity sensors (RH), three thermocouples (T), a mass flow controller (MFC), and four pressure transducers (P), three of which have amaximumoperatingrangeof1000torrandone100torr. . . . . . . . . 77 5.2 Representative diagram of shell and tube membrane with a vacuum ap- pliedtotheshellside. ............................ 79 5.3 Diffusion coefficient for water in Nafion⃝R calculated at various partial pressuresatatemperatureof298K. .................... 82 5.4 Concentration profile for the membrane with a feed relative humidity of 20%andtube-sideflowrateof5slpm. ................... 85 5.5 Concentration profile for the membrane with a feed relative humidity of 20%andtube-sideflowrateof8slpm. ................... 86 5.6 Concentration profile for the membrane with a feed relative humidity of 20%andtube-sideflowrateof10slpm. .................. 87 5.7 Difference between the calculated tube side concentration and the tube sideinterfacialconcentration. ........................ 88 5.8 Concentration profile for the membrane with a feed relative humidity of 50%andtube-sideflowrateof5slpm. ................... 89 5.9 Concentration profile for the membrane with a feed relative humidity of 50%andtube-sideflowrateof8slpm. ................... 90 5.10 Concentration profile for the membrane with a feed relative humidity of 50%andtube-sideflowrateof10slpm. .................. 91 5.11 Concentration profile for the membrane with a feed relative humidity of 70%andtube-sideflowrateof5slpm. ................... 92 5.12 Concentration profile for the membrane with a feed relative humidity of 70%andtube-sideflowrateof8slpm. ................... 93 xPDF Image | TEMPERATURE SWING ADSORPTION COMPRESSION AND MEMBRANE SEPARATIONS
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