Method and apparatus for an on-stream particle replacement syste

Mineral oils: processes and products – Chemical conversion of hydrocarbons – Solids contacting and mixing

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Details

208152, 208173, 208171, 208165, 208166, 208157, 208158, 208163, 208164, C10G 3500

Patent

active

050769081

ABSTRACT:
This invention makes possible substantially continuous flow of uniformly distributed hydrogen and hydrocarbon liquid across a densely packed catalyst bed to fill substantially the entire volume of a reactor vessel by introducing the fluids as alternate annular rings of gas and liquid at a rate insufficient to levitate the bed and with catalyst selected by a density, shape and size at a design feed rate of liquids and gas to prevent ebulation of the packed bed at the design feed rates. Catalysts are selected by measuring bed expansion in a large pilot plant run with hydrocarbon, hydrogen, and catalyst at the design pressures and flow velocities. The liquid and gas components of the feed flow into the bed in alternate annular rings across the full area of the bed. At the desired flow rate, such catalyst continually flows in a plug-like manner downwardly through the vessel by introducing fresh catalyst at the top of the bed by laminarly flowing such catalyst in a liquid stream on a periodic or semicontinuous basis. Catalyst is similarly removed by laminarly flowing catalyst particles in a liquid stream out of the bottom of the bed. Intake for such flow is out of direct contact with the stream of gas flowing through the bed and the flow path is substantially constant in cross-sectional area and greater in diameter by several times than the diameter of the catalyst particles.

REFERENCES:
patent: 3336217 (1967-08-01), Meaux
patent: 3873441 (1975-03-01), Jones
patent: 4540547 (1985-09-01), Schuurman
patent: 4571326 (1986-02-01), Bischoff et al.
patent: 4664782 (1987-05-01), Galiasso et al.

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