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

Operating conditions for 5058 prehydrogenation and 6434 posthydrogenation (in German)

Technical Report ·
OSTI ID:6558898
Data are presented about the processes involved as they were operated. The data include information on starting materials, heats of reaction, throughputs, amounts of circulating gas and cold gas, temperatures, pressures, amounts of water injected, amounts of hydrogen used, amounts of sulfur added, amounts of losses to gas, phenol contents, and characteristics of products (aviation and auto gasolines and middle oils). Among the characteristics of products are mentioned densities, aniline points, chemical compositions, boiling range analyses, and antiknock ratings. In the processes described, the pressure was about 250 atm. The starting material for the 5058 chamber was about 75% fresh middle oil from the liquid phase of coal hydrogenation, about 17% recycled middle oil from the chamber itself, and about 8% gasoline from the liquid phase. The starting material for the 6434 chamber was middle oil or gasoline from the 5058 chamber combined with recycled gasoline from the 6434 chamber itself. The middle oil from the liquid phase had a density of about 0.97 and boiled from about 175/sup 0/C to 325/sup 0/C, whereas the liquid-phase gasoline had density of about 0.74 and boiling range of about 44/sup 0/C to 145/sup 0/C. Auto gasoline from the 5058 chamber had density of about 0.77 and octane number about 70, whereas aviation gasoline from the 5058 chamber had density of about 0.76 and octane number about 75 without lead additive (86 with additive). Corresponding figures for gasoline from the 6434 chamber were 0.74 and 77 for auto gasoline and 0.72 and 76 (89 to 90) for aviation gasoline.
Research Organization:
Hydrierwerke Scholven, A.G., Buer (Germany)
OSTI ID:
6558898
Report Number(s):
TOM-10-269-274
Country of Publication:
United States
Language:
German