METHOD FOR PREPARING A CATALYST USABLE IN HYDROPROCESSING AND HYDROCONVERSION

The invention relates to a method for preparing a catalyst from a catalytic precursor including an alumina and/or silica-alumina and/or zeolite support, and including at least one Group VIB element and optionally at least one Group VIII element, said method involving impregnating said precursor with...

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Hauptverfasser: BERTRAND GUICHARD, LAURENT SIMON, DELPHINE MINOUX, JEAN-PIERRE DATH, VALENTINA DE GRANDI, SYLVIE LOPEZ
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creator BERTRAND GUICHARD
LAURENT SIMON
DELPHINE MINOUX
JEAN-PIERRE DATH
VALENTINA DE GRANDI
SYLVIE LOPEZ
description The invention relates to a method for preparing a catalyst from a catalytic precursor including an alumina and/or silica-alumina and/or zeolite support, and including at least one Group VIB element and optionally at least one Group VIII element, said method involving impregnating said precursor with a solution of a C1-C4 dialkyl succinate. The method comprises a step (step 1) of impregnating said dried, calcined or regenerated precursor with at least one solution containing at least one carboxylic acid other than acetic acid, followed by aging and drying at a temperature of less than or equal to 200°C, optionally followed by a heat treatment at a temperature of less than 350°C, step 1 being followed by impregnation (step 2) with a solution containing at least one C1-C4 dialkyl succinate followed by aging, and drying at a temperature of less than 200°C, without a subsequent calcining step. The catalyst is used in hydroprocessing and/or hydroconversion. La invención se refiere a un proceso para la preparación de un catalizador de un precursor catalítico que comprende un soporte a base de alúmina y/o sílice-alúmina y/o zeolita y que comprende al menos un elemento del grupo VIB y, opcionalmente, al menos un elemento del grupo VIII, el proceso comprende la impregnación del precursor con una solución de un succinato de dialquilo de C1-C4. El proceso comprende una etapa de impregnación (etapa 1) para la impregnación del precursor que está seco, calcinado o regenerado, con al menos una solución que contiene al menos un ácido carboxílico distinto del ácido acético, después la maduración y el secado a una temperatura de menos o igual a 200°C, seguido posiblemente por un tratamiento térmico a una temperatura inferior a 350°C, la etapa 1 está seguida por una etapa de impregnación (etapa 2) con una solución que contiene al menos un succinato de dialquilo de C1- C4 seguido de la maduración y el secado a una temperatura de menos de 200°C sin la siguiente etapa de calcinación. Se utiliza el catalizador en hidrotratamiento y/o hidroconversión.
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The method comprises a step (step 1) of impregnating said dried, calcined or regenerated precursor with at least one solution containing at least one carboxylic acid other than acetic acid, followed by aging and drying at a temperature of less than or equal to 200°C, optionally followed by a heat treatment at a temperature of less than 350°C, step 1 being followed by impregnation (step 2) with a solution containing at least one C1-C4 dialkyl succinate followed by aging, and drying at a temperature of less than 200°C, without a subsequent calcining step. The catalyst is used in hydroprocessing and/or hydroconversion. 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The method comprises a step (step 1) of impregnating said dried, calcined or regenerated precursor with at least one solution containing at least one carboxylic acid other than acetic acid, followed by aging and drying at a temperature of less than or equal to 200°C, optionally followed by a heat treatment at a temperature of less than 350°C, step 1 being followed by impregnation (step 2) with a solution containing at least one C1-C4 dialkyl succinate followed by aging, and drying at a temperature of less than 200°C, without a subsequent calcining step. The catalyst is used in hydroprocessing and/or hydroconversion. 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El proceso comprende una etapa de impregnación (etapa 1) para la impregnación del precursor que está seco, calcinado o regenerado, con al menos una solución que contiene al menos un ácido carboxílico distinto del ácido acético, después la maduración y el secado a una temperatura de menos o igual a 200°C, seguido posiblemente por un tratamiento térmico a una temperatura inferior a 350°C, la etapa 1 está seguida por una etapa de impregnación (etapa 2) con una solución que contiene al menos un succinato de dialquilo de C1- C4 seguido de la maduración y el secado a una temperatura de menos de 200°C sin la siguiente etapa de calcinación. Se utiliza el catalizador en hidrotratamiento y/o hidroconversión.</abstract><oa>free_for_read</oa></addata></record>
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subjects ACYCLIC OR CARBOCYCLIC COMPOUNDS
CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
CHEMISTRY
CRACKING HYDROCARBON OILS
FUELS
LUBRICANTS
METALLURGY
MINERAL WAXES
ORGANIC CHEMISTRY
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
TECHNICAL GASES CONTAINING CARBON MONOXIDE
THEIR RELEVANT APPARATUS
TRANSPORTING
title METHOD FOR PREPARING A CATALYST USABLE IN HYDROPROCESSING AND HYDROCONVERSION
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