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Title: Phase equilibrium in coal liquefaction processes. Final report

Technical Report ·
DOI:https://doi.org/10.2172/6813201· OSTI ID:6813201

Gas-liquid equilibria have been determined in simulation of coal liquefaction process conditions in mixtures of light gases + heavy hydrocarbons (polynuclear aromatics, N, S, and O containing aromatics, some paraffins, and naphthenes). The mixture systems experimentally investigated are: 32 binary mixture systems of a light gas (hydrogen, methane, or carbon dioxide) + a heavy hydrocarbon, 2 ternary mixture systems of hydrogen + two heavy hydrocarbons, 2 ternary mixture systems of hydrogen + methane + a heavy hydrocarbon, 5 complex mixture systems of hydrogen + a coal oil fraction, and 4 complex mixture systems of methane + a coal oil fraction. Equilibrium data were determined at pressures up to 250 atm and temperatures up to 460/sup 0/C which is substantially above the upper limit of previously reported investigations in the literature of about 220/sup 0/C. A flow apparatus of special design made possible the attainment of the elevated temperatures at high pressures. Vapor pressures were determined for eight hydrocarbons at superatmospheric pressures using the same flow apparatus. A solubility parameter based correlation has been developed for the solubility of hydrogen. The hydrogen, methane, and carbon dioxide data have been analyzed and correlated with various degrees of success with the Soave equation of state, and Boublik-Alder-Chen-Kreglewski equation of state.

Research Organization:
Purdue Univ., Lafayette, IN (USA). School of Chemical Engineering
OSTI ID:
6813201
Report Number(s):
EPRI-AP-1593
Country of Publication:
United States
Language:
English