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Ultrafiltration deashing process for Solvent-Refined Coal (SRC)

Conference · · Prepr. Pap., Am. Chem. Soc., Div. Fuel Chem.; (United States)
OSTI ID:6152252
SRC liquid with 1.087 sp gr (90C) and viscosity of 19.8 cp (105C), i.e., a liquefaction product of Indiana V coal consisting of 65% by wt oils (pentane solubles), 27.9% asphaltenes, and 5.7% organic benzene insolubles with 4.5% by wt inorganic ash and 0.55% sulfur content was filtered through a laboratory ultrafiltration (UF) cell under 1-1.55 MPa nitrogen. The UF membranes of a fixed-charge, sulfonic acid type, with approx. 1.5 nm avg pore radius were cast from a solution of polyacrylamide on a spun-bonded polyester support. The steady-state SRC flux through membrane increased by a factor of approx. 2.5 as the liquid viscosity was reduced from 42 to 20.8 by increasing temperature from 85 to 100C. Higher pressures tended to increase the resistance to flow because of the formation of a polarized boundary layer. Both the SRC flux and ash rejection increased and then leveled off as the axial velocity was increased from 3.05 to 3.66 m/sec. Dilution of SRC liquid with 10 or 25% by wt toluene increased the flux by a factor of 3.5 and 6.5, respectively, and improved ash rejection from 99.9 to 99.99-100%. SRC dilution with a coal-derived creosote oil (the 24 CB grade), i.e., a more viscous solvent, was much less effective.
Research Organization:
Columbia University, New York
OSTI ID:
6152252
Report Number(s):
CONF-800814-
Conference Information:
Journal Name: Prepr. Pap., Am. Chem. Soc., Div. Fuel Chem.; (United States) Journal Volume: 25:3
Country of Publication:
United States
Language:
English