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Ultrafiltration de-ashing process for solvent-refined coal

Conference · · Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States)
OSTI ID:6736468
Virtually all of the coal liquefaction processes require the separation of ash particles from the coal derived liquids in order to qualify the product as a furnace fuel. The SRC, Solvent Refined Coal, process produces a liquid having about 5% ash; a reduction of ash to below 0.1% is necessary to obviate the use of electrostatic precipitators in the furnace, thus reducing capital costs in product utilization. A further de-ashing to less than 0.005% would qualify SRC as a gas turbine fuel. Also, since most of the sulfur in SRC (0.55%) is concentrated in the ash; a UF de-ashing process would partially obviate the need for extensive desulfurization of the product. A typical analysis is shown in Table 1. The asphaltenes (benzene soluble, pentane soluble) are believed to be responsible for the high viscosity of the product. A separation of these asphaltenes from the fuel could serve to avert viscosity-related problems in use. These asphaltenes could be further treated by thermal hydrocracking to produce more oil. The objective in this investigation was to study the de-ashing (also de-sulfurization) of SRC using UF membranes including ones of fixed-charge, sulfonic acid nature. Principally such parameters as feed viscosity, temperature, use of solvents, cross-flow velocity, nature of the membrane and its fouling were investigated.
Research Organization:
Columbia Univ., New York, NY
OSTI ID:
6736468
Report Number(s):
CONF-800814-P2
Conference Information:
Journal Name: Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States) Journal Volume: 25:3
Country of Publication:
United States
Language:
English