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U.S. Department of Energy
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Heterogeneous catalytic process for alcohol fuels from syngas. Final technical report

Technical Report ·
DOI:https://doi.org/10.2172/369609· OSTI ID:369609
The primary objective of this project has been the pursuit of a catalyst system which would allow the selective production from syngas of methanol and isobutanol. It is desirable to develop a process in which the methanol to isobutanol weight ratio could be varied from 70/30 to 30/70. The 70/30 mixture could be used directly as a fuel additive, while, with the appropriate downstream processing, the 30/70 mixture could be utilized for methyl tertiary-butyl ether (MTBE) synthesis. The indirect manufacture of MTBE from a coal derived syngas to methanol and isobutanol process would appear to be a viable solution to MTBE feedstock limitations. To become economically attractive, a process fro producing oxygenates from coal-derived syngas must form these products with high selectivity and good rates, and must be capable of operating with a low-hydrogen-content syngas. This was to be accomplished through extensions of known catalyst systems and by the rational design of novel catalyst systems.
Research Organization:
Union Carbide Corp., South Charleston, WV (United States). South Charleston Technical Center
Sponsoring Organization:
USDOE, Washington, DC (United States)
DOE Contract Number:
AC22-91PC90046
OSTI ID:
369609
Report Number(s):
DOE/PC/90046--T18; ON: DE96050287
Country of Publication:
United States
Language:
English