Two-stage coal liquefaction process. Quarterly report, July 1-September 30, 1979
Further evaluation of the macropore catalysts, which have median pore diameters of 2350, 4000, 8800, 12,000 and 15,000 Angstrom have confirmed the previous observation that the macropore catalysts with 2350, 4000, and 8800 Angstroms pores and same pore volume as HDS-1442A, 0.7 cc/g., are capable of higher coal conversion and higher 975/sup 0/F/sup +/ toluene-insoluble residuum conversion than HDS-1442A. Runs carried out at four temperature levels, 780, 810, 830, and 850/sup 0/F establish that the catalyst with 8800 Angstrom pores maintains higher coal conversion and high 975/sup 0/F/sup +/ toluene-insoluble residuum conversion than HDS-1442A at all these four operating temperatures.
- Research Organization:
- Catalysis Research Corp., Palisades Park, NJ (USA)
- OSTI ID:
- 6356473
- Report Number(s):
- FE-3046-T5
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
01 COAL, LIGNITE, AND PEAT
010405* -- Coal
Lignite
& Peat-- Hydrogenation & Liquefaction
CATALYSTS
CHEMICAL PREPARATION
CHEMICAL REACTIONS
COAL LIQUEFACTION
CRYSTAL STRUCTURE
DATA
EXPERIMENTAL DATA
HYDROGENATION
INFORMATION
LIQUEFACTION
MICROSTRUCTURE
NUMERICAL DATA
PERFORMANCE TESTING
POROSITY
SYNTHESIS
TESTING
THERMOCHEMICAL PROCESSES
TSL PROCESS
010405* -- Coal
Lignite
& Peat-- Hydrogenation & Liquefaction
CATALYSTS
CHEMICAL PREPARATION
CHEMICAL REACTIONS
COAL LIQUEFACTION
CRYSTAL STRUCTURE
DATA
EXPERIMENTAL DATA
HYDROGENATION
INFORMATION
LIQUEFACTION
MICROSTRUCTURE
NUMERICAL DATA
PERFORMANCE TESTING
POROSITY
SYNTHESIS
TESTING
THERMOCHEMICAL PROCESSES
TSL PROCESS