Hydrogenation of Lignite with Synthesis Gas
作者:
H. R. APPELL,
E. C. MORONI,
R. D. MILLER,
期刊:
Energy Sources
(Taylor Available online 1977)
卷期:
Volume 3,
issue 2
页码: 163-175
ISSN:0090-8312
年代: 1977
DOI:10.1080/00908317708945977
出版商: Taylor & Francis Group
数据来源: Taylor
摘要:
Lignite may be hydrogenated to a Jow-sulfur, low-ash, heavy fuel oil in the absence of added catalysts by use of synthesis gas and the moisture in the coal as the reducing agent. Conversions of 90-94% and oil yields near 60% (moisture, ash-free basis) have been obtained routinely at temperatures of 425-450°C and pressures of 3000-4000 psig. These conversions and oil yields are higher than those obtained with hydrogen at the same conditions. The effectiveness of carbon monoxide in hydrogenating lignite is, in part, due to the presence of the carbonates of the alkali and alkaline earth metals which react with carbon monoxide, in the presence of water, yielding formates, the active reducing agents.
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