PROCESS FOR PREPARING A HYDROTREATING CATALYST

Process for preparing a hydrotreating catalyst comprising of from 5 wt% to 50 wt% of molybdenum, of from 0.5 wt% to 20 wt% of cobalt, and of from 0 to 5 wt% of phosphorus, all based on total dry weight of catalyst, which process comprises (a) treating a nickel containing carrier with molybdenum, cob...

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Bibliographische Detailangaben
Hauptverfasser:	AZGHAY, ALI, VAN WELSENES, JAN AREND, RIGUTTO, MARCELLO STEFANO, WINTER, FERRY, VAN VLAANDEREN, JOHANNES JACOBUS MARIA, GILTAY, PATRICIA JOHANNA ANNE MARIA
Format:	Patent
Sprache:	eng ; fre
Schlagworte:	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 TECHNICAL GASES CONTAINING CARBON MONOXIDE THEIR RELEVANT APPARATUS TRANSPORTING
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Beschreibung
Zusammenfassung:	Process for preparing a hydrotreating catalyst comprising of from 5 wt% to 50 wt% of molybdenum, of from 0.5 wt% to 20 wt% of cobalt, and of from 0 to 5 wt% of phosphorus, all based on total dry weight of catalyst, which process comprises (a) treating a nickel containing carrier with molybdenum, cobalt and of from 1to 60 %wt of gluconic acid, based on weight of carrier, and optionally phosphorus, (b) optionally drying the treated carrier at a temperature of from 40 to 200 °C, and (c) calcining the treated and optionally dried carrier at a temperature of from 200 to 650 ºC to obtain the calcined treated carrier. L'invention concerne un procédé permettant de préparer un catalyseur d'hydrotraitement, ledit procédé comprenant entre 5 % en poids et 50 % en poids de molybdène, entre 0,5 % en poids et 20 % en poids de cobalt et entre 0 et 5 % en poids de phosphore, toutes ces quantités étant basées sur le poids sec total du catalyseur, lequel procédé consiste à : (a) traiter un support contenant du nickel avec du molybdène, du cobalt et entre 1 et 60 % en poids d'acide gluconique, sur la base du poids du support, et facultativement du phosphore ; (b) facultativement, sécher le support traité à une température comprise entre 40 et 200 °C ; et (c) calciner le support traité et, facultativement, séché, à une température comprise entre 200 et 650 °C pour obtenir le support traité calciné.