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Title: Integration of advanced preparation with coal liquefaction. Third quarterly technical progress report, April 1-June 30, 1984

Technical Report ·
DOI:https://doi.org/10.2172/6754389· OSTI ID:6754389

The objective of this work is to explore the technoeconomic feasibility of a series of unit operations involving: (1) wet grinding of coal in water; (2) removal of chlorine and sodium, release of undesirable mineral matter, and chemical incorporation, if needed, of a disposable liquefaction catalyst in coal via hot water teatment; (3) oil agglomeration to dewater and deash coal while retaining most of the pyrite; and (4) solvent drying of coal agglomerates to eliminate oxidation of coal, improve coal liquefaction reactivity, save energy and prepare the coal/solvent slurry for liquefaction. An apparatus capable of running five microautoclaves simultaneously has been designed and constructed. The autoclaves are shaken along the long axis to insure good mixing and pressure and temperature can be monitored in each autocalve during the run. Reproducibility experiments indicate that the standard deviation on the conversion to THF solubles is about 2.5 percent. The standard deviations in conversions to preasphaltenes and asphaltenes are much higher. A five-autoclave experiment has confirmed earlier results which indicate that wet grinding and hot-water treatment have little effect on conversion to THF solubles but that oil agglomeration followed by drying in a vacuum oven causes a large increase and oil agglomeration followed by solvent drying causes a significant but smaller increase in conversion. 5 references, 13 figures.

Research Organization:
Battelle Columbus Labs., OH (United States)
DOE Contract Number:
AC22-83PC60045
OSTI ID:
6754389
Report Number(s):
DOE/PC/60045-T3; ON: DE84014522
Country of Publication:
United States
Language:
English