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U.S. Department of Energy
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First evaluation of the hydrogenation procesures from primary bitumen (in German)

Technical Report ·
OSTI ID:6728174
Through experimental investigation it was found that direct hydrogenation of bituminous coal with an iron catalyst yielded better overall results with respect to gasoline and middle oil than a two-stage process of extractive hydrogenation at 600 atm followed by hydrogenation of the extract. The two-stage process, however, could be carried out with better yield than the hydrogenation of bituminous coal tar pitch. A comparison of primary bitumen from the 600-atm extractive hydrogenation and bituminous coal tar residue of approximately equal asphalt and high-molecular constituents was made, distinguishing between compositions by the solubilities in benzene and a tetralin-cresol mixture. The primary bitumen had 1.2% insolubles in a tetralin-cresol mixture as compared to 14.0% for the coal tar residue. The benzene-insoluble portion minus the tetralin-cresol insolubles was 16.2% of the primary bitumen and 8.6% of the tar residue. Asphalt content were 24.9% for bitumen and 18.8% for the tar. These results indicated a greater heavy oil content produced from the primary bitumen than the tar residue. Lowering the temperature gave a better asphalt and solid decomposition. Gas production was low at 11%. It was also shown that the direct hydrogenation was more favorable as far as low gasification, higher yield, and oil production were concerned. The gasoline production was lower at 23.2% as compared with 27.0% for the two-stage process. It was thought that the two-stage process could be advantageous for the production of heavy oil, where there would be a very low loss to gasification. 1 table
Research Organization:
I.G. Farbenindustrie, A.G., Ludwigshafen (Germany)
OSTI ID:
6728174
Report Number(s):
TOM-162-164-166
Country of Publication:
United States
Language:
German