Exchanger Cont

Fig. 14.4. (cont.) respect to exchange of the two hydrogen atoms. The dashed contours in the top panel represent the PES in the excited electronic state. In contrast to Figure 13.3 we show here the wavefunction rather than its modulus square ... 

Alongi, D.M., Tirendi, F., and Christoffersen, P. (1993) Sedimentary profiles and sediment-water solute exchange of iron and manganese in reef- and river-dominated shelf regions of the Coral Sea. Cont. Shelf Res. 13, 287-305. 

Walsh, J.J., Biscaye, P.E., and Csanady, G.T. (1988) The 1983-1984 shelf-edge exchange processes (SEEP)—I. Experiment hypothesis and highlights. Cont. Shelf Res. 8, 435-456. 

AUer, R. C., Mackin, J. E., UUman, W. J., Wang, C., Tsai, S., Jin, J., Sui, Y., and Hong, J. (1985). Early chemical diagenesis, sediment—water solute exchange, and storage of reactive organic matter near the mouth of the Changjiang, East China Sea. Cont. Shelf Res. 4, 227—251. 

Apel FN, Conte LB, Bender HL (1964) Cationic exchanging polymeric resin. US Patent 3,153,001, 13 Oct 1964, to Union Carbide. 

TABLE 6 B73 STANDARDIZED ELECTRONIC DATA EXCHANGE FILE SPECIFICATION (CONT D)... 

Figure 6. Lead breakthrough curve on Na-exchanged chabazite tuff bed, treated by 28 mg-1 Ij b solution, cont inin 23 mg-1 Na, 4 mg-1 K, 60 mg-1 Ca and 24 m -l Mg, as interfering cations. Feed flow rate 10.8 ml-min...

The acid properties of SAPO-5 samples can be modified either by the con x>sition of framework, or by ion-exchange or impregnation. These changes in the acid properties can have certain implications on the catalytic performances. This assertion is proved by the results shown in Figure 3, where it can be observed that the decrease of the phosphorus cont t and partially of the aluninium determines an increase of the activity, but the selectivity is kept constant. The difference between the framework compositions deter-... 

Conte et al. 2001, Zhou 2005). AuxUiary equipment is required to manage the storage heat exchange should be provided by a mineral oU, in order to remove the heat of adsorption and to provide the heat of desorption. 

Usage conditions when employing ion exchangers or sacrificial anodes for drinking water treatment (cont.)... 

---