BR112018076203A2 - catalisador de craqueamento catalítico fluidizado de zeólita, método para reduzir o coque de contaminação e os rendimentos de hidrogênio e método de craqueamento catalítico de matérias primas de hidrocarbonetos pesados - Google Patents

catalisador de craqueamento catalítico fluidizado de zeólita, método para reduzir o coque de contaminação e os rendimentos de hidrogênio e método de craqueamento catalítico de matérias primas de hidrocarbonetos pesados

Info

Publication number
BR112018076203A2
BR112018076203A2 BR112018076203-2A BR112018076203A BR112018076203A2 BR 112018076203 A2 BR112018076203 A2 BR 112018076203A2 BR 112018076203 A BR112018076203 A BR 112018076203A BR 112018076203 A2 BR112018076203 A2 BR 112018076203A2
Authority
BR
Brazil
Prior art keywords
catalytic
cracking catalyst
catalytic cracking
coke
zeolite
Prior art date
Application number
BR112018076203-2A
Other languages
English (en)
Other versions
BR112018076203B1 (pt
Inventor
Mcguire Robert
M. Smith Gary
Yilmaz Bilge
Serneels Sven
Original Assignee
Basf Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Basf Corporation filed Critical Basf Corporation
Publication of BR112018076203A2 publication Critical patent/BR112018076203A2/pt
Publication of BR112018076203B1 publication Critical patent/BR112018076203B1/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084—Y-type faujasite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/51—Spheres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/612—Surface area less than 10 m2/g
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/613—10-100 m2/g
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/615—100-500 m2/g
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/205—Metal content

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

é fornecido um catalisador de craqueamento catalítico fluidizado de zeólita que passiva níquel e vanádio durante o craqueamento catalítico. o catalisador de craqueamento catalítico fluidizado de zeólita inclui y-faujasita cristalizada in situ a partir de uma microesfera calcinada que contém metacaulim. o catalisador de craqueamento catalítico fluidizado de zeólita inclui ainda uma matriz que contém alumina obtida através da calcinação de uma boemita cristalina dispersível e um caulim contido na microesfera calcinada que contém metacaulim, em que a boemita cristalina dispersível possui um tamanho de cristalita inferior a 500 å. também são fornecidos um método para reduzir o coque de contaminação e os rendimentos de hidrogênio e um método de craqueamento catalítico de matérias primas de hidrocarbonetos pesados.
BR112018076203-2A 2016-06-17 2017-06-16 Catalisador de craqueamento catalítico fluidizado de zeólita e uso de um catalisador de craqueamento catalítico fluidizado de zeólita BR112018076203B1 (pt)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US201662351602P 2016-06-17 2016-06-17
US62/351,602 2016-06-17
US15/264,428 US10633596B2 (en) 2016-06-17 2016-09-13 FCC catalyst having alumina derived from crystalline boehmite
US15/264,428 2016-09-13
PCT/US2017/037853 WO2017218879A1 (en) 2016-06-17 2017-06-16 Fcc catalyst having alumina derived from crystalline boehmite

Publications (2)

Publication Number Publication Date
BR112018076203A2 true BR112018076203A2 (pt) 2019-03-26
BR112018076203B1 BR112018076203B1 (pt) 2022-11-08

Family

ID=60661665

Family Applications (1)

Application Number Title Priority Date Filing Date
BR112018076203-2A BR112018076203B1 (pt) 2016-06-17 2017-06-16 Catalisador de craqueamento catalítico fluidizado de zeólita e uso de um catalisador de craqueamento catalítico fluidizado de zeólita

Country Status (7)

Country Link
US (2) US10633596B2 (pt)
EP (1) EP3472270A4 (pt)
JP (1) JP7021121B2 (pt)
KR (1) KR102431720B1 (pt)
CN (1) CN109312238B (pt)
BR (1) BR112018076203B1 (pt)
WO (1) WO2017218879A1 (pt)

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* Cited by examiner, † Cited by third party
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US10633596B2 (en) * 2016-06-17 2020-04-28 Basf Corporation FCC catalyst having alumina derived from crystalline boehmite
US11529618B2 (en) 2016-11-28 2022-12-20 Basf Se Catalyst composite comprising an alkaline earth metal containing CHA zeolite and use thereof in a process for the conversion of oxygenates to olefins
CN110636901A (zh) * 2017-05-17 2019-12-31 巴斯夫公司 底部残留物改质和低焦炭流化催化裂化催化剂
US20230294988A1 (en) 2020-05-29 2023-09-21 Basf Se Catalyst for hydrogen chloride oxidation and production thereof
US20230365424A1 (en) * 2020-09-29 2023-11-16 Basf Corporation Crystalline boehmite materials as precursors for large crystal gamma alumina and low surface area alpha alumina

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Also Published As

Publication number Publication date
WO2017218879A1 (en) 2017-12-21
RU2019100950A (ru) 2020-07-17
CN109312238B (zh) 2021-08-27
US20170362513A1 (en) 2017-12-21
US11254878B2 (en) 2022-02-22
JP2019523705A (ja) 2019-08-29
EP3472270A4 (en) 2020-04-08
US10633596B2 (en) 2020-04-28
JP7021121B2 (ja) 2022-02-16
BR112018076203B1 (pt) 2022-11-08
RU2019100950A3 (pt) 2020-08-18
KR20190018493A (ko) 2019-02-22
KR102431720B1 (ko) 2022-08-11
CN109312238A (zh) 2019-02-05
US20200224102A1 (en) 2020-07-16
EP3472270A1 (en) 2019-04-24

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B06W Patent application suspended after preliminary examination (for patents with searches from other patent authorities) chapter 6.23 patent gazette]
B350 Update of information on the portal [chapter 15.35 patent gazette]
B07A Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

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