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1. WO2022005544 - FCC CATALYST COMPOSITIONS FOR FLUID CATALYTIC CRACKING AND METHODS OF USING THE FCC CATALYST COMPOSITIONS

Publication Number WO/2022/005544
Publication Date 06.01.2022
International Application No. PCT/US2021/024620
International Filing Date 29.03.2021
IPC
B01J 29/08 2006.1
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
29Catalysts comprising molecular sieves
04having base-exchange properties, e.g. crystalline zeolites, pillared clays
06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
08of the faujasite type, e.g. type X or Y
B01J 29/40 2006.1
BPERFORMING OPERATIONS; TRANSPORTING
01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
29Catalysts comprising molecular sieves
04having base-exchange properties, e.g. crystalline zeolites, pillared clays
06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
40of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
C10G 47/20 2006.1
CCHEMISTRY; METALLURGY
10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
47Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, to obtain lower boiling fractions
02characterised by the catalyst used
10with catalysts deposited on a carrier
12Inorganic carriers
16Crystalline alumino-silicate carriers
20the catalyst containing other metals or compounds thereof
Applicants
  • SAUDI ARABIAN OIL COMPANY [SA]/[SA]
  • ARAMCO SERVICES COMPANY [US]/[US] (AG)
  • JGC CATALYSTS AND CHEMICALS LTD [JP]/[JP]
  • JAPAN COOPERATION CENTER PETROLEUM [JP]/[JP]
Inventors
  • KOSEOGLU, Omer Refa
  • JIN, Yaming
  • USHIO, Masaru
  • ARAKAWA, Seiji
Agents
  • CAMPBELL, Quinten M.
  • BEYER, James E.
  • FANE, Brian M.
  • LUNN, Jennifer H.
  • MCNEELY, Richard J.
  • MEYER, Christopher I.
  • MOLLOY, Matthew A.
  • POWELL, Carolyn S.
  • REED, John D.
  • THARP, Amy M.
Priority Data
16/919,33602.07.2020US
Publication Language English (en)
Filing Language English (EN)
Designated States
Title
(EN) FCC CATALYST COMPOSITIONS FOR FLUID CATALYTIC CRACKING AND METHODS OF USING THE FCC CATALYST COMPOSITIONS
(FR) COMPOSITIONS DE CATALYSEUR DE CRAQUAGE CATALYTIQUE FLUIDE (FCC) POUR CRAQUAGE CATALYTIQUE FLUIDE ET PROCÉDÉS D'UTILISATION DES COMPOSITIONS DE CATALYSEUR FCC
Abstract
(EN) A fluid catalytic cracking catalyst composition (FCC catalyst composition) includes a framework-substituted ultra-stable Y-type zeolite (USY zeolite) having one or more transition metals substituted into the framework of a USY zeolite and a FCC zeolite cracking additive. A method for upgrading a hydrocarbon feed includes contacting the hydrocarbon feed with the FCC catalyst composition of the present disclosure at reaction conditions sufficient to upgrade at least a portion of the hydrocarbon feed. A method for upgrading a hydrocarbon feed includes passing the hydrocarbon feed to a fluid catalytic cracking unit, contacting the hydrocarbon feed with a FCC catalyst composition in the fluid catalytic cracking unit under reaction conditions sufficient to cause at least a portion of the hydrocarbon feed to undergo cracking reactions to produce a cracking reaction mixture comprising a used FCC catalyst composition and a cracked effluent comprising one or more olefins.
(FR) L'invention concerne une composition de catalyseur de craquage catalytique fluide (composition de catalyseur FCC) comprend une zéolite de type Y ultra-stable substituée par une structure (zéolite USY) ayant un ou plusieurs métaux de transition substitués dans le cadre d'une zéolite USY et d'un additif de craquage à zéolite FCC. Un procédé de valorisation d'une charge d'hydrocarbures comprend la mise en contact de la charge d'hydrocarbures avec la composition de catalyseur FCC de la présente invention dans des conditions de réaction suffisantes pour valoriser au moins une partie de la charge d'hydrocarbures. Un procédé de valorisation d'une charge d'hydrocarbure comprend le passage de la charge d'hydrocarbure vers une unité de craquage catalytique fluide, la mise en contact de la charge d'hydrocarbures avec une composition de catalyseur FCC dans l'unité de craquage catalytique de fluide dans des conditions de réaction suffisantes pour amener au moins une partie de la charge d'hydrocarbures à subir des réactions de craquage pour produire un mélange de réaction de craquage comprenant une composition de catalyseur FCC usé et un effluent craqué comprenant une ou plusieurs oléfines.
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