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

Process for coal liquefaction

Patent ·
OSTI ID:6401626
The invention provides a process for the liquefaction of coal. The comminuted coal is slurried in a solvent or pasting oil and digested, normally under hydrogen pressure, e.g. of 50 to 250 atmospheres partial pressure, under catalytic conditions, at temperatures between about 380 and 500/sup 0/C., preferably 400 to 470/sup 0/C. And residence times between about 10 and 100 minutes. Solvent or pasting oil is obtained wholly or mostly by recycling from the distilled fractionation of the reaction products. The solvent system comprises a light fraction in the boiling range up to 200/sup 0/C. And a heavy residue fraction, boiling mainly above 450/sup 0/C., there being a more or less well-defined lack of solvent in a boiling range intermediate between 200 and 450/sup 0/C. Preferably less than 20%, e.g. 5% or less of the solvent system boils between 200 and 450/sup 0/C. The ratio of low boiling to high boiling solvent is preferably from about 3:1 to 1:3. The process can be controlled so that the coal is converted virtually completely into distillable products, more particularly predominantly in the crude diesel fuel range (200 to 450/sup 0/C.). Optionally fractionating residue may be recovered as a further valuable product for making exceptionally high grade electrodes by delayed coking at 500/sup 0/C. Followed by graphitization at 1400/sup 0/C.
Assignee:
Sasol One Pty Ltd (South Africa)
Patent Number(s):
US 4251346
OSTI ID:
6401626
Country of Publication:
United States
Language:
English