METHOD AND APPARATUS FOR WITHDRAWAL OF SMALL CATALYST PARTICLES IN FCC SYSTEMS

IMPROVED METHOD AND APPARATUS FOR WITHDRAWAL OF SMALL CATALYST PARTICLES IN FCC SYSTEMS Disclosed is a method of and apparatus for reducing the level of extremely small catalyst particles ("fines") in an FCC system by temporarily retaining particles separated from the secondary cyclone sep...

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Hauptverfasser: SCHATZ, KLAUS W, OWEN, HARTLEY, HADDAD, JAMES H
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creator SCHATZ, KLAUS W
OWEN, HARTLEY
HADDAD, JAMES H
description IMPROVED METHOD AND APPARATUS FOR WITHDRAWAL OF SMALL CATALYST PARTICLES IN FCC SYSTEMS Disclosed is a method of and apparatus for reducing the level of extremely small catalyst particles ("fines") in an FCC system by temporarily retaining particles separated from the secondary cyclone separator in a reactor vessel or catalyst regenerator, These particles can be intermittently withdrawn from the temporary retaining area in order to achieve particle flow at a low volume rate, which takes them out of the active catalyst inventory within the reactor/regenerator system. The intermittent withdrawing of catalyst "fines" reduces the particulate contamination both in flue gas exhausted to the atmosphere from the catalyst regenerator and in the main column bottom (MCB) products from the fractionation stage. Preferred embodiments include intermittent withdrawal of "fines" from either the regenerator or the reactor vessels and the secondary cyclones contained in each of these vessels.
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The intermittent withdrawing of catalyst "fines" reduces the particulate contamination both in flue gas exhausted to the atmosphere from the catalyst regenerator and in the main column bottom (MCB) products from the fractionation stage. 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The intermittent withdrawing of catalyst "fines" reduces the particulate contamination both in flue gas exhausted to the atmosphere from the catalyst regenerator and in the main column bottom (MCB) products from the fractionation stage. 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The intermittent withdrawing of catalyst "fines" reduces the particulate contamination both in flue gas exhausted to the atmosphere from the catalyst regenerator and in the main column bottom (MCB) products from the fractionation stage. Preferred embodiments include intermittent withdrawal of "fines" from either the regenerator or the reactor vessels and the secondary cyclones contained in each of these vessels.</abstract><edition>5</edition><oa>free_for_read</oa></addata></record>
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language eng ; fre
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subjects BLASTING
CHEMISTRY
CRACKING HYDROCARBON OILS
FUELS
FURNACES
FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL
HEATING
KILNS
LIGHTING
LUBRICANTS
MECHANICAL ENGINEERING
METALLURGY
MINERAL WAXES
OPEN SINTERING OR LIKE APPARATUS
OVENS
PEAT
PETROLEUM, GAS OR COKE INDUSTRIES
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
RETORTS
TECHNICAL GASES CONTAINING CARBON MONOXIDE
WEAPONS
title METHOD AND APPARATUS FOR WITHDRAWAL OF SMALL CATALYST PARTICLES IN FCC SYSTEMS
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