WO2024184704 - FEEDSTOCK TO AROMATIC HYDROCARBONS CONVERSION VIA FORMALDEHYDE ROUTE IN DUAL BED REACTOR

National phase entry is expected:
Publication Number WO/2024/184704
Publication Date 12.09.2024
International Application No. PCT/IB2024/050602
International Filing Date 22.01.2024
Title **
[English] FEEDSTOCK TO AROMATIC HYDROCARBONS CONVERSION VIA FORMALDEHYDE ROUTE IN DUAL BED REACTOR
[French] CHARGE D'ALIMENTATION POUR CONVERSION D'HYDROCARBURES AROMATIQUES PAR VOIE DE FORMALDÉHYDE DANS UN RÉACTEUR À DOUBLE LIT
Applicants **
KING ABDULLAH UNIVERSITY OF SCIENCE AND TECHNOLOGY 4700 King Abdullah University of Science and Technology Thuwal 23955-6900, SA
Inventors
LI, Teng 4700 King Abdullah University of Science and Technology Thuwal 23955-6900, SA
RUIZ-MARTINEZ, Javier 4700 King Abdullah University of Science and Technology Thuwal 23955-6900, SA
Priority Data
63/450,770   08.03.2023   US
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Quotation for National Phase entry

Country StagesTotal
China Filing1353
EPO Filing, Examination8445
Japan Filing531
South Korea Filing575
USA Filing, Examination2635
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Total: 13539

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

Abstract[English] A catalytic kit (710) for converting a feedstock to aromatics in a dual bed reactor includes a first catalyst A1 configured to promote (1) a conversion of a first part of the feedstock into olefins and (2) a conversion of diene and the olefines into the aromatics; a second catalyst A2 configured to promote a conversion of a second part of the feedstock into formaldehyde; and a third catalyst B configured to promote a conversion of olefines into additional aromatics, where the first and second catalysts A1, A2 are mixed together to be in direct contact with each other.[French] L'invention concerne un kit catalytique (710) pour convertir une charge d'alimentation en aromatiques dans un réacteur à double lit qui comprend un premier catalyseur A1 conçu pour favoriser (1) une conversion d'une première partie de la charge d'alimentation en oléfines et (2) une conversion de diène et des oléfines en composés aromatiques ; un second catalyseur A2 conçu pour favoriser une conversion d'une seconde partie de la charge d'alimentation en formaldéhyde ; et un troisième catalyseur B conçu pour favoriser une conversion d'oléfines en aromatiques supplémentaires, les premier et second catalyseurs A1, A2 étant mélangés ensemble pour être en contact direct l'un avec l'autre.
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