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Kinetics and FTIR studies of hydrocarbon synthesis on Pd/ZSM5 catalysts. Final report

Technical Report ·
OSTI ID:7043461
Hydrocarbon synthesis during CO hydrogenation over Pd/M-ZSM5 (M=H,Na,La) and Pd/SiO/sub 2/ has been investigated. Overall activity depended on the cation-exchanged form of the support and decreased in the order Pd/La-ZSM5 = Pd/Na-ZSM5 > Pd/H-ZSM5 > Pd/SiO/sub 2/. The zeolite-supported catalysts showed high selectivity towards saturated C/sub 2/-C/sub 6/ hydrocarbons, whereas Pd/SiO/sub 2/ favored methanol production. Increasing temperature and H/sub 2//CO feed ratio led to higher reaction rates, lower yields of C/sub 2/-C/sub 6/ products, and increased lighter hydrocarbons. A mechanical mixture of Pd/SiO/sub 2/ and Na-ZSM5 showed similar product distribution as Pd/Na-ZSM5. Infrared spectra of the catalysts under reaction conditions indicate the presence of adsorbed oxygenates on the zeolite. Changes in the IR bands during the initial stages of the reaction suggest that surface species on the zeolite are not methanol synthesis intermediates. The effects of various temperatures and H/sub 2//CO ratios on the spectra are small. The kinetic and infrared results indicate that C/sub 2/+ hydrocarbons synthesis over Pd/ZSM5 follows a bifunctional reaction pathway, involving methanol synthesis over Pd and conversion of methanol to hydrocarbons on the zeolite support. 33 refs., 15 figs., 3 tabs.
Research Organization:
Notre Dame Univ., IN (USA). Dept. of Chemical Engineering
DOE Contract Number:
FG22-84PC70788
OSTI ID:
7043461
Report Number(s):
DOE/PC/70788-T5; ON: DE87001708
Country of Publication:
United States
Language:
English

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