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U.S. Department of Energy
Office of Scientific and Technical Information

Patent application for a process for hydrogenation of pitch from low-temperature carbonization of bituminous coal. [Effects of catalyst on product proportions] (in German)

Technical Report ·
OSTI ID:7307679
The beginning material for the process was pitch dissolved in middle oils or heavy oils from previous runs, and a solid catalyst was used. The starting material was filtered to remove any ash present, then was heated to some temperature less than 300/sup 0/C in a preheater and then mixed in the reaction oven with hydrogen gas, which had been heated to a very high temperature in its own preheater, so that the temperature in the reaction oven became about 460/sup 0/C, with a hydrogen partial pressure of up to 700 atm. The pitch contained 30 to 40 percent asphalt, which might have precipitated out and choked the system, but it was prevented from doing that by the rather low temperature in the preheater and the fact that the catalyst converted all the asphalt to lower-molecular-weight materials. The catalyst used depended on the ultimate products desired. For products low in hydrogen and rich in aromatics, a small amount of hydrogenating metals (molybdenum, chromium, etc.) or metal compounds carried on a substance such as siliceous earth, silica gel, alumina, or activated charcoal, which had strong splitting effects, was used, whereas to obtain hydrogen-rich products, more of the metal, or even nothing but the metal, was used. From a typical run of the process, one could expect to obtain 10 percent gaseous products, 5 percent water, 10 percent gasoline, 20 percent middle oils, and 55 percent heavy oils.
Research Organization:
Ruhroel, G.m.b.H., Bottrop (Germany)
OSTI ID:
7307679
Report Number(s):
TOM-8-52-55
Country of Publication:
United States
Language:
German