WO2025078612 - METHOD FOR PRODUCING COLORLESS HYDROCARBON PRODUCT WITH LOW CARBON INTENSITY

National phase entry is expected:
Publication Number WO/2025/078612
Publication Date 17.04.2025
International Application No. PCT/EP2024/078706
International Filing Date 11.10.2024
Title **
[English] METHOD FOR PRODUCING COLORLESS HYDROCARBON PRODUCT WITH LOW CARBON INTENSITY
[French] PROCÉDÉ DE PRODUCTION D'UN PRODUIT HYDROCARBONÉ INCOLORE À FAIBLE INTENSITÉ DE CARBONE
Applicants **
TOPSOE A/S
Inventors
LEJRE, Kasper Hartvig Lyng
COSTA, Ignacio Fabian
MORTEN, Krogh Johansen
Priority Data
23203526.1   13.10.2023   EP
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Quotation for National Phase entry

Country StagesTotal
China Filing, Examination, Granting1909
EPO Filing, Examination, Granting8113
Japan Filing, Examination, Granting2029
South Korea Filing, Examination, Granting1819
USA Filing, Examination, Granting4740
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Total: 18,610

The term for entry into the National Phase has expired. This quotation is for informational purposes only

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Abstract[English] The disclosure relates to a process wherein a hydrocarbonaceous feedstock and a gas comprising hydrogen contacts a hydroprocessing catalyst, such as an isomerization catalyst or a hydrocracking catalyst under active hydroprocessing conditions to provide a hydroprocessed process stream, wherein the hydroprocessed process stream contacts a catalyst comprising an aluminosilicate characterized in the entire hydroprocessed process stream is directed to be cooled by at least 20°C prior to contacting a hydrogenation catalyst.[French] L'invention concerne un procédé dans lequel une charge d'alimentation hydrocarbonée et un gaz comprenant de l'hydrogène entrent en contact avec un catalyseur d'hydrotraitement, tel qu'un catalyseur d'isomérisation ou un catalyseur d'hydrocraquage dans des conditions d'hydrotraitement actives pour fournir un flux de traitement hydrotraité, ledit flux de traitement hydrotraité entrant en contact avec un catalyseur comprenant un aluminosilica. Ledit procédé est caractérisé en ce que l'ensemble du flux de traitement hydrotraité soit dirigé pour être refroidi d'au moins 20 °C avant sa mise en contact avec un catalyseur d'hydrogénation.