Method for converting loads from renewable sources using a catalyst including an Nu-10 zeolite and a silica-alumina

Converting a paraffinic feedstock constituted of 9-25C hydrocarbons using a catalyst comprising a hydro-dehydrogenated metal consisting of group VIB metals and/or VIII group metals and a support comprising a zeolite Nu-10 and silica alumina, is claimed. The paraffinic feedstock is produced from rene...

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Bibliographic Details
Main Authors Martens, Johan, Marques Mota, Filipe Manuel, Duchene, Pascal, Bouchy, Christophe
Format Patent
LanguageEnglish
French
German
Published 08.05.2019
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
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Summary:Converting a paraffinic feedstock constituted of 9-25C hydrocarbons using a catalyst comprising a hydro-dehydrogenated metal consisting of group VIB metals and/or VIII group metals and a support comprising a zeolite Nu-10 and silica alumina, is claimed. The paraffinic feedstock is produced from renewable resources, and is obtained by Fischer-Tropsch process. The method is carried out: at a temperature of 150-500[deg] C, a pressure of 0.1-15 MPa and a hourly space velocity of 0.1-10 h->1>; and in presence of hydrogen. The ratio between hydrogen and feedstock is 70-2000 Nm3>/m3>.
Bibliography:Application Number: EP20140305339