Method of operation of the present vapor phase in the Leuna Works

Technical Report · Thu Jan 16 04:00:00 EST 1941

OSTI ID:7320663

Ibing, G

Some significant data are given about the 5058 chamber, the 6434 chamber, the refining of gasoline, and the gasoline variety VT702. The 5058 chamber used a loading of 0.8 to 1.0 kg/l/hr, temperature of 19 to 22 mV, and starting material of lignite A-middle oils, with density (D/sub 4//sup 20/) being 0.910, aniline point +15/sup 0/C, distillation beginning 70/sup 0/C and ending 325/sup 0/C, phenol content 10 percent, and hydrogen content 10.0 to 10.5 percent. The resulting product from the separator had density 0.8000 to 0.805, distillation cutoff 120/sup 0/ for gasoline (20 to 25 percent distilling up to that point), aniline point 55/sup 0/, and phenol content less than 0.5 percent by weight. The 6434 chamber used a loading of 0.8 kg/l/hr, temperature of 20 to 24 mV, and starting material consisting of a 1:1 mixture of 5058 and 6434 B-middle oils, with density 0.800, aniline point 50 to 55/sup 0/C, distillation beginning 120/sup 0/C and ending 320/sup 0/C, phenol content 0.3 to 0.4 percent (due to added H/sub 2/S). In producing aviation gasoline, the yield was about 78 percent of the A-product, whereas in producing auto gasoline, it was about 90 percent. The product from the separator had density 0.750 to 0.760, distillation cutoff 140/sup 0/C for gasoline (45 percent distilling up to that point), aniline point 50 to 55/sup 0/C, and phenol content 0.02 percent (which was maintained at that level for inhibitor effect). The gasoline VT702 had density 0.720, aniline point 50 to 52/sup 0/C, and octane numbers of 71 to 72 before and 90.5 to 91.5 after addition of 1.2 tetraethyl-lead. It contained 5 to 7 percent aromatics, 2 to 3 percent olefins, 40 percent naphthenes, and 50 to 53 percent paraffin. The distillation cutoff was 140 to 145/sup 0/C, and 65 percent of the product distilled up to 100/sup 0/C. The sulfur content was less than 0.001 percent.

• Research Organization: Ruhroel, G.m.b.H., Bottrop (Germany)
• OSTI ID: 7320663
• Report Number(s): TOM-7-580-582
• Country of Publication: United States
• Language: German

Related Subjects

01 COAL, LIGNITE, AND PEAT
010403 -- Coal & Coal Products-- Hydrogenation-- (-1987)
010405* -- Coal
Lignite
& Peat-- Hydrogenation & Liquefaction
010600 -- Coal
Lignite
& Peat-- Properties & Composition
ANTIKNOCK RATINGS
BROWN COAL
CARBONACEOUS MATERIALS
CATALYSTS
CHEMICAL ANALYSIS
CHEMICAL COMPOSITION
CHEMICAL REACTION YIELD
CHEMICAL REACTIONS
COAL
COAL LIQUEFACTION
COAL LIQUIDS
ENERGY SOURCES
FOSSIL FUELS
FUELS
GASOLINE
GERMANY
HIGH PRESSURE
HIGH TEMPERATURE
HYDROGENATION
LIGNITE
LIQUEFACTION
PETROLEUM PRODUCTS
QUANTITATIVE CHEMICAL ANALYSIS
THERMOCHEMICAL PROCESSES
YIELDS