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674 A. Malekpour, A. Samadi-Maybodi and M. R. Sadati 13.6 13.5 13.4 13.3 13.2 13.1 13 12.9 12.8 12.7 99.35 99.30 99.25 99.20 99.15 99.10 99.05 flux rejection 012345 time (h) 6.8 6.75 6.7 6.65 6.6 6.55 6.5 99.79 99.78 99.78 99.77 99.77 99.76 99.76 99.75 99.75 flux rejection 012345 time (h) (a) (b) 12.6 12.55 12.5 12.45 12.4 12.35 12.3 12.25 99.38 99.36 99.34 99.32 99.30 99.28 99.26 99.24 99.22 flux rejection 012345 time (h) (c) Figure 5: Flux and ion rejection vs. time for ionic solutions through a NaA membrane a) Cs+; b) Sr2+ ; c) I- 3 2.95 2.9 2.85 2.8 2.75 2.7 2.65 99.62 99.6 99.58 99.56 99.54 99.52 99.5 99.48 99.46 99.44 99.42 flux rejection 012345 time (h) 1.45 1.4 1.35 1.3 1.25 1.2 1.15 99.995 99.99 99.985 99.98 99.975 99.97 99.965 012345 time (h) flux rejection (a) (b) 2.55 2.5 2.45 2.4 2.35 2.3 2.25 2.2 2.15 99.56 99.54 99.52 99.5 99.48 99.46 99.44 flux rejection 012345 time (h) (c) Figure 6: Flux and ion rejection vs. time for ionic solutions through a ZSM-5 membrane a) Cs+; b) Sr2+; c) I- Brazilian Journal of Chemical Engineering flux (mol m-2 h-1) fflux (mol m-2 h-1)) ion rejection (%) ion rejection (%) flux (mol m-2 h-1) flux (mol m-2 h-1) ion rejection (%) flux (mol m-2 h-1) ion rejection (%) ion rejection (%) ion rejection (%) flux (mol m-2 h-1)PDF Image | DESALINATION OF AQUEOUS SOLUTIONS ZEOLITE MEMBRANES
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