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Exploratory studies in catalytic coal liquefaction. Final report, June 1978-March 1979

Technical Report ·
DOI:https://doi.org/10.2172/5768251· OSTI ID:5768251
HRI, has run catalyst aging tests simulating H-coal conditions with Illinois No. 6 coal for approx. 10 days with Cyanamid 1442A (CoMo/Al/sub 2/O/sub 3/), Cyanamid NiMo/Al/sub 3/O/sub 3/, Armak NiMo/Al/sub 2/O/sub 3/, Amocat 1A (CoMo/Al/sub 2/O/sub 3/), and Amocat 1B (Mo/Al/sub 2/O/sub 3/) catalysts. From each test we obtained fresh catalyst, aged catalyst from the end of the run, and total reactor effluents (less gases) from various times during the run. In a test developed at Mobil using a fixed bed, high pressure downflow reactor and model compound mixtures, we examined fresh and aged catalysts for hydrogenation, hydrocracking, isomerization, desulfurization, denitrogenation, and deoxygenation. Several minerals were also included in the tests. Activities, selectivities and deactivation are discussed. Fresh commercial catalysts, especially NiMo/Al/sub 2/O/sub 3/, appear to be undesirably active for the H-Coal process. Amocat 1B is the least active. All catalysts age extensively but the used catalysts are still quite active. Activities for all reactions are reduced in the presence of nitrogen compounds. Hydrocracking activity appears to be critical to denitrogenation effectiveness. Examination of the products of the HRI catalyst aging runs confirms the interpretations of the model compound tests. Also, it is found that 400/sup 0/F/sup +/ product mixtures become more complex as catalysts age, and that the catalysts affect especially the highest (largest size) boiling products, but lose the ability to lower molecular weight as they age. A brief examination of novel hydrogen donor-catalyst systems is also described.
Research Organization:
Mobil Research and Development Corp., Princeton, NJ (USA)
OSTI ID:
5768251
Report Number(s):
EPRI-AF-1184
Country of Publication:
United States
Language:
English