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Title: Low severity upgrading of F-T waxes with solid superacids

Technical Report ·
DOI:https://doi.org/10.2172/6855179· OSTI ID:6855179

In the past year, we synthesized a Pt/ZrO[sub 2]/SO[sub 4] catalyst which exhibits high conversions and selectivity for desirable products from long-chain paraffins, such as n-hexadecane, n-dotriacontane(n-C[sub 32]) and a SASOL wax(C[sub 58]-C[sub 64]). The catalyst preparation procedure has been carefully worked out and is reproducible. Isomerization and hydrocracking activities of long-chain paraffins and selectivities to various products were examined under mild conditions: 443 K and 2.5 MPa initial hydrogen pressure. Effects of temperature, pressure, catalyst loading, Pt concentration on n-alkane conversions were studied to understand the mechanism on the acid catalyst surface. Upgrading of the alkanes proceeds through initial isomerization followed by [beta]-scission reactions and further isomerizations. Isomerization is favored at low temperature and short reaction times, whereas cracking is favored at higher temperatures or pressures. The hydrogen pressure has a considerable influence on the product distribution. Hydrogen transfer probably proceeds through dissociation of molecular hydrogen to generate pretonic acid sites which cause C-C cleavage. Effect of increasing Pt loadings shows a trend similar to increasing hydrogen pressure. Characterization of the present catalyst demonstrates that catalytic activity depends to a large extent on proper coordination of finely dispersed platinum to strong acid sites as well as on pore size distribution.

Research Organization:
Pittsburgh Univ., PA (United States). Dept. of Chemical and Petroleum Engineering
Sponsoring Organization:
USDOE; USDOE, Washington, DC (United States)
DOE Contract Number:
FG22-91PC91304
OSTI ID:
6855179
Report Number(s):
DOE/PC/91304-T4; ON: DE93008123
Country of Publication:
United States
Language:
English