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5.13 Concentration profile for the membrane with a feed relative humidity of 70%andtube-sideflowrateof10slpm. .................. 94 5.14 Flux of water through the membrane for a tube-side flow rate of 5 slpm. Symbols are used to delineate curves and do not represent measured data. 96 5.15 Flux of water through the membrane for a tube-side flow rate of 8 slpm. Symbols are used to delineate curves and do not represent measured data. 97 5.16 Fluxofwaterthroughthemembraneforatube-sideflowrateof10slpm. Symbols are used to delineate curves and do not represent measured data. 98 6.1 Diagram of the apparatus for the removal of water vapor using a shell and tube Nafion⃝R multi-tube membrane module under counter-current operation which uses three relative humidity sensors (RH), four thermo- couples (T), two mass flow meters (FM), two pressure transducers (P), andadewpointsensor(DP)......................... 105 6.2 Representative diagram of shell and tube membrane under counter-current operation.................................... 108 6.3 Water concentration profile along the length of the membrane for a tube siderelativehumidityof33%andaVs/Vt ratioof1.1. . . . . . . . . . . 115 6.4 Water concentration profile along the length of the membrane for a tube siderelativehumidityof45%andaVs/Vt ratioof1.1. . . . . . . . . . . 116 6.5 Water concentration profile along the length of the membrane for a tube siderelativehumidityof45%andaVs/Vt ratioof1.1. . . . . . . . . . . 117 6.6 Difference between the calculated bulk concentration on the tube and shell side and their corresponding interfacial concentrations. . . . . . . . . . . 118 6.7 Flux of water through the membrane for various relative humidities and aVs/Vtratioof1.1. ............................. 119 6.8 Temperature profile along the length of the membrane for a tube side relativehumidityof33%andaVs/Vt ratioof1.1. . . . . . . . . . . . . . 120 xiPDF Image | TEMPERATURE SWING ADSORPTION COMPRESSION AND MEMBRANE SEPARATIONS
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