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U.S. Department of Energy
Office of Scientific and Technical Information

Enhanced catalysis by solvent improvement. Quarterly technical progress report, 1 January-31 March 1984

Technical Report ·
OSTI ID:7043555

This report describes the results obtained by liquefying Illinois No. 6 coal with base liquefaction and modified solvents. Liquefaction conditions such as reaction temperature, time, initial hydrogen pressure, solvent-to-coal ratio, catalyst concentration, and type of catalyst were varied to determine their effect upon liquefaction, and to identify the reaction conditions that increase oil yields. The experimental results showed that increasing reaction temperature from 425 to 440/sup 0/C in the presence of 500 ppM molybdenum catalyst based on coal significantly increased gas yield when modified solvent was used. Both oil yield and conversion, however, decreased with increasing temperature, indicating an onset of retrogressive reaction at higher temperatures. This onset may have been due to limited hydrogen transfer either from the gas to liquid phase or from the liquid phase to thermally produced molecular fragments from the coal. The effect of these limitations on coal liquefaction was investigated by changing the initial hydrogen pressure and solvent-to-coal ratio. Catalytic coal liquefaction experiments showed that the addition of 125 ppM molybdenum based on coal significantly increased both oil yield and coal conversion over those noted in noncatalytic liquefaction with modified solvent. Both oil yield and conversion increased even more when the molybdenum concentration increased from 125 to 250 ppM. However, a further increase to 500 ppM did not cause any noticeable improvement. 9 tabs.

Research Organization:
Air Products and Chemicals, Inc., Allentown, PA (USA)
DOE Contract Number:
AC22-82PC50003
OSTI ID:
7043555
Report Number(s):
DOE/PC/50003-32; ON: DE87002238
Country of Publication:
United States
Language:
English