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Transference number, mll11llter/f tH+ =0.8 tCl- =0.2 tH 0 =130 2 tH+ =0.6 tCl- =0.4 tH 0 =130 2 Number o f cycles 1 5 10 20 45 1 5 10 End o f - ac bD C 0 C 0 C 0 C D C D C D C 0 C D C 0 C D SOlut~~ volume, Ionlc concentratlon gradlent across Hydrogen concentratlon gradlent across membrane, &J+. 9 lon/llter 1 . 4 -0 1.34 - . 0 2 1.32 - . 0 3 1.l4 - . 1 5 1.44 -.28 .14 .12 -.02 .09 -.03 .14 .12 -.02 .09 -.03 1.45 -0 tH+=0.2 1 867 997 857 987 844 974 1026 72 -0 tCl- =0.8 5 tH0=130 10 2 tH+ "' 0.2 tCl- =0.8 1 C 918 1082 -111 0 998 1002 98 5 C 912 1088 -118 -0 acharge. bD1Scharge. TABLE 13. - CALCULATED EFFECT OF TRANSFERENCE NUMBERS ON OSMOTIC PRESSURE AND H+ CONCENTRATION DIfFERENCES (WATER TRANSPORT TOWARD CHROMIUM ELECTRODE) 1 C 0 918 1082 131 998 1002 98 912 1088 125 5 C membrane, Fe Cr UC 867 997 857 987 844 974 792 922 753 883 867 997 857 987 844 974 1133 1003 1143 1013 1156 1026 1208 1078 1246 1117 tH+ =0.8 tCl- = 0.2 tH 0 =80 2 tH+ =0.6 tCl- = 0.4 tH 0 = 80 2 0984101583-.04 9 lon/flter 76x10- 2 97 63 85 50 72 -10 15 -55 -29 1133 1003 1143 1013 85 1156 -33 1026 72 1133 -169 1003 97 1143 -181 1013 85 1156 -197 1.03 0992100891 -0 10 C 904 1096 115 0 984 1015 83 20 C 888 1112 ~9 0 968 1032 64 1.42 - . 0 4 1.42 - . 0 6 1.03 0 998 1002 98 -0 1 C 918 108~ 50 5C912108844 1.03 0992100891 -0 10 C 904 1096 35 1.02 20 C 888 1112 17 [J 968 1032 64 . 9 8 - . 0 7 .24 .22 10 C 904 1096 -126 .21 0992100891 -0 tH 0 = 80 2 0984101583-.04 30 C 872 1128 -163 .15 D 952 1048 48 - . 1 0 -6 97 -18 -0PDF Image | NASA Redox Storage System Development Project 1980
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