GAS-LIQUID SEPARATION DEVICE WITH A ZONE FOR GUIDING THE LIQUID AT THE OUTLET END, IN PARTICULAR FOR A THREE-PHASE FLUIDISED BED REACTOR

The invention relates to a gas-liquid separation device, in particular for use in the recirculation zone of three-phase fluidised bed reactors. The gas-liquid separation device comprises a plurality of separation elements, each having an inlet duct (70) and a succession of at least two bends (71, 72...

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Hauptverfasser: BALZ, Pierre, AIT-MHAND, Driss, LE COZ, Jean-François, AMBLARD, Benjamin, VINCENT-GENOD, Vanessa, BRAHEM, Rim, MARQUES, Joao
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creator BALZ, Pierre
AIT-MHAND, Driss
LE COZ, Jean-François
AMBLARD, Benjamin
VINCENT-GENOD, Vanessa
BRAHEM, Rim
MARQUES, Joao
description The invention relates to a gas-liquid separation device, in particular for use in the recirculation zone of three-phase fluidised bed reactors. The gas-liquid separation device comprises a plurality of separation elements, each having an inlet duct (70) and a succession of at least two bends (71, 72), a first bend (71) located in the plane (zy), the axis of the first bend (71) forming an orientation angle a relative to the vertical axis z of between 45° and 315°, and a second bend (72) forming a second orientation angle p with the first bend (71) of between 1° and 135°. The two first successive bends (71, 72) are separated by a distance D1 of between D/2 and 4D, D being the diameter of the inlet duct (70). Each separation element comprises a liquid guidance device (73) which is positioned at the outlet end of the second bend (72), and which has an open section.
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The gas-liquid separation device comprises a plurality of separation elements, each having an inlet duct (70) and a succession of at least two bends (71, 72), a first bend (71) located in the plane (zy), the axis of the first bend (71) forming an orientation angle a relative to the vertical axis z of between 45° and 315°, and a second bend (72) forming a second orientation angle p with the first bend (71) of between 1° and 135°. The two first successive bends (71, 72) are separated by a distance D1 of between D/2 and 4D, D being the diameter of the inlet duct (70). Each separation element comprises a liquid guidance device (73) which is positioned at the outlet end of the second bend (72), and which has an open section.</abstract><oa>free_for_read</oa></addata></record>
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subjects CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
CHEMISTRY
CRACKING HYDROCARBON OILS
FUELS
LUBRICANTS
METALLURGY
MINERAL WAXES
PEAT
PERFORMING OPERATIONS
PETROLEUM, GAS OR COKE INDUSTRIES
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION
RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES
REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS
REFORMING OF NAPHTHA
SEPARATION
TECHNICAL GASES CONTAINING CARBON MONOXIDE
THEIR RELEVANT APPARATUS
TRANSPORTING
title GAS-LIQUID SEPARATION DEVICE WITH A ZONE FOR GUIDING THE LIQUID AT THE OUTLET END, IN PARTICULAR FOR A THREE-PHASE FLUIDISED BED REACTOR
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