Hydrogen consumption data during the hydrogenation of Scholven and Welheim middle oil using the Ruhroel catalyst K413

Technical Report · Sat Apr 12 04:00:00 EST 1941

OSTI ID:7307668

Hydrogenation of the gasoline-free Scholven middle oil was done at a temperature of 501/sup 0/C, a pressure of 540 atm, and a load of 1.0 kg/liter/hr. There was 66.28 kg C in A middle oil, 52.9 kg C in gasoline including 14.19 kg gasified, and 17.55 kg hydrocarbons. There were 641 m/sup 3/ of hydrogen consumed during production of one ton of gasoline from gasoline-free middle oil. Hydrogenation of the gasoline containing Scholven middle oil was done at a temperature of 501/sup 0/C, pressure of 540 atm, and a load of 1.45 kg/liter/hr. There was 95.4 kg C in A middle oil, 75.25 kg C in gasoline, 20.15 kg gasified C with a carbon number of 2.94, and 24.65 kg of hydrocarbons. There were 527 m/sup 3/ of H/sub 2/ consumed during production of one ton of gasoline from gasoline-containing Scholven middle oil. Hydrogenation of the Welheim middle oil took place at a temperature of 501/sup 0/C, pressure of 630 atm, and a load of 1.06 tons/m/sup 3/hr. The data used were taken from a report dated December 24, 1940. There were 9955 kg C in A middle oil, 8477 kg C in gasoline, 1478 kg gasified carbon with a carbon number of 2.54, and a 1820 kg hydrocarbons. There were 610 m/sup 3/H/sub 2/ consumed during production of one ton of gasoline from Welheim coal tar gasoline.

• Research Organization: Ruhroel, G.m.b.H., Bottrop (Germany)
• OSTI ID: 7307668
• Report Number(s): TOM-237-143-145
• Country of Publication: United States
• Language: English

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010403* -- Coal & Coal Products-- Hydrogenation-- (-1987)
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CHEMICAL REACTIONS
COAL LIQUEFACTION
COAL LIQUIDS
CONSUMPTION RATES
CRYOGENIC FLUIDS
ELEMENTS
FLUIDS
FUELS
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