Mild hydrocracking of an unstable feedstock in a three-phase fluidized-bed reactor: behavior of the process and of the chemical compounds
The mild hydrocracking (400[degrees]C, 125 atm) of an unstable feedstock (shale oil) was performed in a three-phase fluidized-bed reactor with a commercial sulfided Ni-Mo catalyst. The hydroprocessing was monitored with respect to the physicochemical properties and the chemical composition of the na...
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Veröffentlicht in: | Industrial & engineering chemistry research 1992-09, Vol.31 (9), p.2127-2133 |
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Sprache: | eng |
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