Separation of Fischer-Tropsch wax from catalyst by supercritical extraction. Quarterly report, July 1, 1996 - September 30, 1996
Author(s) -
Patrick C. Joyce,
Mark C. Thies,
D. Sherrard,
J. Biales,
Peter K. Kilpatrick,
Greg Roberts
Publication year - 1996
Publication title -
osti oai (u.s. department of energy office of scientific and technical information)
Language(s) - English
Resource type - Reports
DOI - 10.2172/467814
Subject(s) - wax , supercritical fluid , extraction (chemistry) , fischer–tropsch process , supercritical fluid extraction , slurry , catalysis , chemical engineering , bubble column reactor , solubility , hydrocarbon , solvent , hexane , chemistry , chromatography , materials science , organic chemistry , bubble , composite material , engineering , parallel computing , gas bubble , computer science , selectivity
The objective of this research projects is to evaluate the potential of SCF extraction for separating the catalyst slurry of a Fischer- Tropsch (F-T) slurry bubble column (SBC) reactor into two fractions: (1) a catalyst-free wax containing less than 10 ppm particulate matter and (2) a concentrated catalyst slurry that is ready for recycle or regeneration. The wax will be extracted with a hydrocarbon solvent that has a critical temperature near the operating temperature of the SBC reactor, i.e. 200-300{degrees}C. Initial work is being performed using n-hexane as the solvent. The success of the projects depends on two major factors. First, the supercritical solvent must be able to dissolve the F-T wax; furthermore, the must be accomplished without entraining the solid catalyst. Second, the extraction must be controlled so as not to favor the removal of the low molecular weight wax compounds, i.e., a constant carbon-number distribution of the alkanes in the wax slurry must be maintained at steady-state column operation. The project includes three tasks (1) equilibrium solubility measurements, (2) thermodynamic modeling, and (3) process design studies
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