Desulfurization of Transportation Fuels with Zeolites Under Ambient Conditions
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A. Avidan M. Cullen paper AM-01-55 presented at the National Petroleum and Refiners Association Annual Meeting Washington DC 18 to 20 March 2001.
B. C. Gates J. R. Katzer G. C. A. Schuit Chemistry of Catalytic Processes (McGraw-Hill New York 1979) chap. 5.
R. T. Yang Adsorbents: Fundamentals and Applications (Wiley New York 2003) chap. 10. This reference contains a detailed review of the literature of all commercial and nontraditional sorbents that have been tested as well as the different approaches for deep desulfurization of transportation fuels.
The calculations were performed at the Hartree-Fock and density functional theory level using effective core potentials ( 11 ). The restricted Hartree-Fock theory at the LanL2DZ level basis set ( 12 ) was used to determine the geometries and the adsorption bonding energies ( 8 ). Natural bond orbital analysis at the B3LYP/LanL2DZ level was used for studying the electron density distribution of the adsorption system ( 8 ). A cluster model was used to represent zeolite framework structure to which Ag + and Cu + cations were bonded.
The adsorber bed contained 1 to 2 g of zeolite and the feed flow rate was maintained at 0.5 cm 3 /min. Effluent (or eluent) samples were collected at regular intervals until saturation was reached and the samples were subsequently analyzed for sulfur-containing compounds with a gas chromatograph (GC) equipped with a flame photometric detector (FPD). The FPD was operated at a sensitivity (or detection limit) of 0.02 ppmw sulfur. Fourier transform infrared spectroscopy was used for analysis of aromatic and aliphatic contents by means of the C-H stretching bands.
Fuel Cells for Transportation 2001 Annual Report (U.S. Department of Energy Office of Transportation Technologies Washington DC 2001).
This work was funded by NSF and the U.S. Department of Energy. U.S. and foreign patents are pending.