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DESULFURIZATION OF TRANSPORTATION FUELS  349

                        Table 10.13. Example of heteroatom contents in the FCC
                        gasoline
                        Heteroatoms                    Content, ppmw

                        Nitrogen                            16.0
                        Oxygen                              14.0
                        Mercaptan sulfur                    24.2
                        Sulfide sulfur                        7.3
                        Thiophene sulfur                    61.9
                        C 1 thiophene sulfur               115.0
                        C 2 thiophene sulfur               130.6
                        C 3 thiophene sulfur                90.9
                        C 4 thiophene sulfur                88.0
                        Benzothiophene and                 238.1
                          dibenzothiophene sulfur
                                    Total                  786.0

                        Irvine, 1998.


              From these analyses, the sorbent to be developed must have the highest affini-
            ties for the thiophenic compounds, medium affinities for the aromatics, and lowest
            possible affinities for the alkanes and branched alkanes.

            10.7.2. Sorbents Studied or Used

            The use of sorbents for sulfur removal dates back to the use of bauxite (i.e.,
            the ore for aluminum smelting) to adsorb mercaptans from various petroleum
            fractions (Purdy, 1958). Red mud (the iron-rich waste from the Bayer process
            for alumina extraction from bauxite) has also been used as a sorbent for sulfur
            removal from petroleum oils.
              The recent search for sorbents for liquid fuel desulfurization has taken two
            paths, both based on trial-and-error. One approach has been simply testing the
            commercial sorbents. The other approach has an origin in HDS catalysis. This
            approach is aimed at sorbents that are good catalysts for HDS, with the hope
            that such sorbents would form a bond with the sulfur atom of the thiophenic
            compounds. Forming such a bond may require above-ambient temperatures. The
            commercialized process discussed above, SZorb, is based on an interesting
            hybrid of catalyst and sorbent. The use of π-complexation is an entirely different
            approach and will be discussed separately.
              The commercial sorbents (activated carbon, activated alumina, and zeolites)
            have all been studied for sulfur removal. The zeolites included 5A; 13X (Salem,
            1994; Salem and Hamid, 1997); various ZSM’s, including ZSM-5 and silicalite
            (Weitkamp et al., 1991); and ion-exchanged zeolites (Michlmayr, 1980; Vansant
            et al., 1988). The ion exchange was intended for the exchanged cation to form a
            bond with the sulfur atom in thiophene. Although some of these sorbents showed
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