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U.S. Department of Energy
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Fundamental studies of catalytic gasification: Quarterly report, October 1, 1987-December 31, 1987

Technical Report ·
OSTI ID:5151234

In the catalytic steam gasification of chars, North Dakota lignite char was selected for an investigation of ash component-catalyst interaction because of its high mineral content. Both nickel and potassium seem to react with minerals in the ash, greatly reducing catalytic activity of the nickel-potassium catalyst. Ash components initially catalyze gasification in the absence of an added catalyst, but this activity rapidly declines with time. When a nickel-potassium catalyst is added to the char after its gasification activity has ceased, gasification resumes with good activity and steady state gas production until almost all carbonaceous matter has been gasified. Demineralization of the char by HCl/HF treatment resulted in a char which had no catalytic activity of its own, but which was easily gasified after impregnation with Ni/K catalyst. Gasification proceeded at steady state and without the poisoning of activity observed in the presence of mineral matter. Potassium appears to interact with calcium in the ash giving an eutecticum which wets the carbon and acts as a gasification catalyst, which is superior to either potassium or calcium alone in the absence of ash. Alkali earth-alkali mixtures must therefore be investigated as potential catalysts. Nickel alone is very sensitive to the ash content of the char, apparently due to interaction between nickel and either calcium and/or sulfur. It has almost no activity for gasifying the North Dakota char in contrast to a short lived high level activity in the gasification of graphite and of low ash chars. 17 refs, 4 figs., 4 tabs.

Research Organization:
Lawrence Berkeley Lab., CA (USA)
DOE Contract Number:
AC03-76SF00098
OSTI ID:
5151234
Report Number(s):
LBL-24531; ON: DE88008391
Country of Publication:
United States
Language:
English