Page 368 - Adsorbents fundamentals and applications
P. 368

DESULFURIZATION OF TRANSPORTATION FUELS  353

                        Table 10.16. Summary of energies of adsorption (E)for
                        thiophene and benzene in kcal/mol, calculated from mo-
                        lecular orbital theory
                        Sorbent      E ads (Thiophene)  E ads (Benzene)

                          + −
                        Cu Z             21.4               20.5
                          + −
                        Ag Z             20.0               19.1
                        (Z −  denotes zeolite anion using the cluster model shown in
                        Figure 8.3; From Yang et al., 2002.)


              Ab initio molecular orbital calculations were performed for the bonding be-
                                          +
                                                  +
            tween benzene or thiophene with Cu and Ag exchanged zeolites (Yang et al.,
            2002; Takahashi et al., 2002). The results on energy calculations are summarized
            in Table 10.16. As described in Chapter 8, the energy predictions from ab initio
            methods (e.g., at high levels of basis sets of Gaussian) are fairly accurate. The
            calculations showed that the π-complexation bonds for thiophene are stronger
            than that with benzene, and that Cu(I)Y adsorbs more strongly than AgY does;
            that is, the relative strengths of the π-complexation bonds follow:

                           For the same sorbate: Cu > Ag +
                                                +
                           For the same sorbent: thiophene > benzene

            Furthermore, the predicted bond strengths in the neighborhood of 20 kcal/mol
            are well-suited for purification.
              Vapor-phase adsorption isotherms of benzene and thiophene on various sor-
            bents including CuY and AgY were measured first in order to assess their
            suitabilities for sulfur removal, as well as for the removal of aromatics. Direct
            correlations have yet to be established between the vapor-phase isotherms and
            the liquid-phase isotherms. However, some efforts have already been made in
            this direction by using the potential theory approach where log (C s /C) replaces
            log (P s /P ) in the potential energy expression (C s is the saturated concentration
            in solution and P s is the saturated vapor pressure, see Manes, 1998). A sorbent
            capable of adsorbing thiophene at very low partial pressures in the gas phase
            should also be able to do so in the liquid phase.

            NaY, AgY, and Cu(I)Y. Figure 10.53 shows the equilibrium isotherms of ben-
                                                   ◦
            zene and thiophene on NaY at 120 and 180 C. More benzene was adsorbed
            on NaY than thiophene at pressures <10 −2  atm. From Table 10.15, benzene
            has a higher polarizability. This result indicates that the van der Waals interac-
            tions and the interaction between the field (of Na ) and induced dipole domi-
                                                      +
            nated the adsorption; both interactions depend on the polarizability (see Chap-
            ter 2). At higher pressures over 1 × 10 −2  atm, pore filling occurred and the
            benzene adsorption amount became smaller because benzene has a larger molar
            volume than that of thiophene. Na-Y does not have selectivity for thiophene;
   363   364   365   366   367   368   369   370   371   372   373