MX378472B - Soportes de alúmina que contienen sílice, catalizadores elaborados a partir de éstos y procesos que los utilizan. - Google Patents

Soportes de alúmina que contienen sílice, catalizadores elaborados a partir de éstos y procesos que los utilizan.

Info

Publication number
MX378472B
MX378472B MX2014007351A MX2014007351A MX378472B MX 378472 B MX378472 B MX 378472B MX 2014007351 A MX2014007351 A MX 2014007351A MX 2014007351 A MX2014007351 A MX 2014007351A MX 378472 B MX378472 B MX 378472B
Authority
MX
Mexico
Prior art keywords
processes
same
catalysts made
made therefrom
containing alumina
Prior art date
Application number
MX2014007351A
Other languages
English (en)
Other versions
MX2014007351A (es
Inventor
Bruno C Nesci
Cecelia A Radlowski
Gill M Malick
Jifei Jia
Roberto Romero
Xianghua Yu
Original Assignee
Advanced Refining Technologies Llc
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=48669342&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=MX378472(B) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Advanced Refining Technologies Llc filed Critical Advanced Refining Technologies Llc
Publication of MX2014007351A publication Critical patent/MX2014007351A/es
Publication of MX378472B publication Critical patent/MX378472B/es

Links

Classifications

    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19—Molybdenum
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F7/00—Compounds of aluminium
    • C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12—Silica and alumina
    • 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
    • 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
    • B01J35/63—Pore volume
    • 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
    • B01J35/63—Pore volume
    • B01J35/635—0.5-1.0 ml/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
    • B01J35/64—Pore diameter
    • 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
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/66—Pore distribution
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • B01J37/0207—Pretreatment of the support
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/03—Precipitation; Co-precipitation
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00—Silicon; Compounds thereof
    • C01B33/113—Silicon oxides; Hydrates thereof
    • C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/12—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Catalysts (AREA)
  • Nanotechnology (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Se describen composiciones de soporte de alúmina que contienen al menos 0.1% en peso de sílice. El soporte de alúmina se caracteriza por un volumen de poro mayor de 0.60 cm3/g, una mediana del tamaño de poro que abarca desde aproximadamente 70 hasta aproximadamente 120, una distribución del tamaño de poro para que al menos 90% del volumen de poro total caiga dentro del intervalo de aproximadamente 20 hasta aproximadamente 250, y una amplitud de la distribución del tamaño de poro de no menos de aproximadamente 40. Las composiciones de alúmina de la presente invención exhiben un modo del pico primario en un diámetro de poro menor que la mediana del diámetro de poro. También se proporcionan catalizadores preparados a partir de los soportes de alúmina y los procesos para preparar y utilizar los soportes y los catalizadores.
MX2014007351A 2011-12-22 2012-11-20 Soportes de alúmina que contienen sílice, catalizadores elaborados a partir de éstos y procesos que los utilizan. MX378472B (es)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201161579357P 2011-12-22 2011-12-22
US201261587872P 2012-01-18 2012-01-18
PCT/US2012/066107 WO2013095856A1 (en) 2011-12-22 2012-11-20 Silica containing alumina supports, catalysts made therefrom and processes using the same

Publications (2)

Publication Number Publication Date
MX2014007351A MX2014007351A (es) 2014-11-25
MX378472B true MX378472B (es) 2025-03-11

Family

ID=48669342

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2014007351A MX378472B (es) 2011-12-22 2012-11-20 Soportes de alúmina que contienen sílice, catalizadores elaborados a partir de éstos y procesos que los utilizan.

Country Status (11)

Country Link
US (2) US11090638B2 (es)
EP (1) EP2794088B1 (es)
JP (1) JP6134334B2 (es)
KR (1) KR102041652B1 (es)
CN (1) CN104114273B (es)
BR (1) BR112014015372B1 (es)
CA (1) CA2860166C (es)
MX (1) MX378472B (es)
SG (1) SG11201403322XA (es)
TW (1) TWI641554B (es)
WO (1) WO2013095856A1 (es)

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JP6134334B2 (ja) 2011-12-22 2017-05-24 アドバンスド・リフアイニング・テクノロジーズ・エルエルシー シリカ含有アルミナ担体、それから生じさせた触媒およびそれの使用方法
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FR3022255B1 (fr) * 2014-06-13 2016-07-29 Ifp Energies Now Procede d'hydrotraitement de coupes distillats utilisant un catalyseur a base d'une alumine mesoporeuse amorphe ayant une connectivite elevee
FR3022158B1 (fr) * 2014-06-13 2018-02-23 IFP Energies Nouvelles Catalyseur mesoporeux d'hydroconversion de residus et methode de preparation
FR3022254B1 (fr) * 2014-06-13 2016-07-29 Ifp Energies Now Procede d'hydrotraitement de coupes gazoles utilisant un catalyseur a base d'une alumine mesoporeuse amorphe ayant une connectivite elevee
FR3022156B1 (fr) * 2014-06-13 2018-02-23 Ifp Energies Now Catalyseur mesoporeux et macroporeux a phase active comalaxee, son procede de preparation et son utilisation en hydrotraitement de residus
FR3022160B1 (fr) * 2014-06-13 2021-05-07 Ifp Energies Now Catalyseur a phase active de nickel comalaxee mesoporeux et macroporeux ayant un diametre median macroporeux compris entre 50 et 300 nm et son utilisation en hydrogenation
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Also Published As

Publication number Publication date
WO2013095856A1 (en) 2013-06-27
CA2860166C (en) 2017-08-22
TWI641554B (zh) 2018-11-21
JP2015508380A (ja) 2015-03-19
MX2014007351A (es) 2014-11-25
BR112014015372A8 (pt) 2017-06-13
US20210362137A1 (en) 2021-11-25
US11090638B2 (en) 2021-08-17
SG11201403322XA (en) 2014-07-30
CA2860166A1 (en) 2013-06-27
BR112014015372B1 (pt) 2020-01-14
JP6134334B2 (ja) 2017-05-24
EP2794088B1 (en) 2021-03-31
TW201341314A (zh) 2013-10-16
US11642664B2 (en) 2023-05-09
CN104114273B (zh) 2018-05-15
KR20140106710A (ko) 2014-09-03
KR102041652B1 (ko) 2019-11-06
EP2794088A4 (en) 2015-09-09
EP2794088A1 (en) 2014-10-29
US20140367311A1 (en) 2014-12-18
CN104114273A (zh) 2014-10-22
BR112014015372A2 (pt) 2017-06-13

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