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Development of liquid-phase catalysts for brown coals. Report on a discussion in Leuna on January 26, 1944 (in German)

Technical Report ·
OSTI ID:6176665
Leuna operated brown coal hydrogenation without a catalyst from 1927 until 1929, but achieved decomposition rates of only about 60%. After 1929 they used catalysts consisting either of molybdenum compounds or iron compounds. If the brown coal were treated with 25% of the amount of sulfuric acid necessary for complete neutralization of the brown coal, an addition of 0.05% (based on amount of coal) molybdic acid (MoO/sub 3/), added as an ammonium salt, would work very well as a catalyst. Later an iron sulfate catalyst neutralized by alkali and carried on brown-coal coke (Me 10927) was found to be effective at the level of 0.8% iron based on amount of coal. The active agent was hypothesized to be iron sulfide formed with the sulfur of the coal through an intermediate iron hydroxide from the alkalization. Just as scarcity of molybdenum encouraged the switch to iron catalysts, the limitations of supply of iron sulfate caused the usage of more plentiful types of iron compounds, mainly oxides, arising as by-products of aluminum manufacture or other processes. Some of these compounds were Bayermasse, Luxmasse, and Lautamasse. However, it took about 1.8% iron in the form of Bayermasse, for instance, to have the same effect as 0.8% iron in the form of iron sulfate. For the hydrogenation of bituminous coal, Ludwigshafen had experimented with iron sulfate and Bayermasse together, (in fact 0.2% iron in iron sulfate and 0.4% iron in Bayermasse), obtaining satisfactory catalyst action when used with Sulfigran (sodium sulfide).
Research Organization:
Hydrierwerke Poelitz, A.G. (Germany)
OSTI ID:
6176665
Report Number(s):
TOM-75-638-639
Country of Publication:
United States
Language:
German