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FR3022161B1 - Catalyseur a phase active de nickel comalaxee mesoporeux et macroporeux ayant un diametre median macroporeux superieur a 300 nm et son utilisation en hydrogenation - Google Patents

Catalyseur a phase active de nickel comalaxee mesoporeux et macroporeux ayant un diametre median macroporeux superieur a 300 nm et son utilisation en hydrogenation Download PDF

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Publication number
FR3022161B1
FR3022161B1 FR1455430A FR1455430A FR3022161B1 FR 3022161 B1 FR3022161 B1 FR 3022161B1 FR 1455430 A FR1455430 A FR 1455430A FR 1455430 A FR1455430 A FR 1455430A FR 3022161 B1 FR3022161 B1 FR 3022161B1
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FR
France
Prior art keywords
macroporeous
active phase
nickel
catalyst
comalaxed
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Active
Application number
FR1455430A
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English (en)
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FR3022161A1 (fr
Inventor
Malika Boualleg
Anne-Claire Dubreuil
Emily Maille
Cecile Thomazeau
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IFP Energies Nouvelles IFPEN
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IFP Energies Nouvelles IFPEN
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Priority to FR1455430A priority Critical patent/FR3022161B1/fr
Priority to EP15730988.1A priority patent/EP3154686A1/fr
Priority to PCT/EP2015/062817 priority patent/WO2015189191A1/fr
Priority to CN201580031619.1A priority patent/CN106604978B/zh
Priority to RU2017100932A priority patent/RU2683776C2/ru
Priority to US15/318,611 priority patent/US10258969B2/en
Publication of FR3022161A1 publication Critical patent/FR3022161A1/fr
Application granted granted Critical
Publication of FR3022161B1 publication Critical patent/FR3022161B1/fr
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32Selective hydrogenation of the diolefin or acetylene compounds
    • C10G45/34Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
    • C10G45/36Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02Boron or aluminium; Oxides or hydroxides thereof
    • B01J21/04Alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/755Nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/393Metal or metal oxide crystallite size
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/61310-100 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
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    • B01J35/643Pore diameter less than 2 nm
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    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
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    • B01J35/653500-1000 nm
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66Pore distribution
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/009Preparation by separation, e.g. by filtration, decantation, screening
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0236Drying, e.g. preparing a suspension, adding a soluble salt and drying
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
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    • B01J37/03Precipitation; Co-precipitation
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    • B01J37/03Precipitation; Co-precipitation
    • B01J37/036Precipitation; Co-precipitation to form a gel or a cogel
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • BPERFORMING OPERATIONS; TRANSPORTING
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    • BPERFORMING OPERATIONS; TRANSPORTING
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    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16Reducing
    • BPERFORMING OPERATIONS; TRANSPORTING
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/03Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
    • CCHEMISTRY; METALLURGY
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    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/03Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
    • C07C5/05Partial hydrogenation
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    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
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    • C07C5/10Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of aromatic six-membered rings
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32Selective hydrogenation of the diolefin or acetylene compounds
    • C10G45/34Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
    • C10G45/40Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing platinum group metals or compounds thereof
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/44Hydrogenation of the aromatic hydrocarbons
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    • C10G45/48Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
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    • C10GCRACKING 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/44Hydrogenation of the aromatic hydrocarbons
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    • C10G45/52Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing platinum group metals or compounds thereof
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • C07C2523/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
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    • C07C2601/00Systems containing only non-condensed rings
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    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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Abstract

L'invention concerne un catalyseur comprenant une matrice oxyde majoritairement aluminique calcinée et une phase active comprenant du nickel, ladite phase active étant au moins en partie comalaxée au sein de ladite matrice oxyde majoritairement aluminique calcinée, la teneur en nickel étant comprise entre 5 et 65 % poids dudit élément par rapport à la masse totale du catalyseur, ladite phase active ne comprenant pas de métal du groupe VIB, les particules de nickel ayant un diamètre inférieur à 15 nm, ledit catalyseur ayant un diamètre médian mésoporeux compris entre 8 et 25 nm, un diamètre médian macroporeux supérieur à 300 nm, un volume mésoporeux mesuré par porosimétrie au mercure supérieur ou égal à 0,30 mL/g et un volume poreux total mesuré par porosimétrie au mercure supérieur ou égal à 0,34 mL/g. L'invention concerne également le procédé de préparation dudit catalyseur et son utilisation dans un procédé d'hydrogénation.
FR1455430A 2014-06-13 2014-06-13 Catalyseur a phase active de nickel comalaxee mesoporeux et macroporeux ayant un diametre median macroporeux superieur a 300 nm et son utilisation en hydrogenation Active FR3022161B1 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
FR1455430A FR3022161B1 (fr) 2014-06-13 2014-06-13 Catalyseur a phase active de nickel comalaxee mesoporeux et macroporeux ayant un diametre median macroporeux superieur a 300 nm et son utilisation en hydrogenation
EP15730988.1A EP3154686A1 (fr) 2014-06-13 2015-06-09 Catalyseur mesoporeux et macroporeux a base de nickel obtenu par comalaxage et ayant un diametre median macroporeux superieur a 300 nm et son utilisation en hydrogenation d'hydrocarbures
PCT/EP2015/062817 WO2015189191A1 (fr) 2014-06-13 2015-06-09 Catalyseur mesoporeux et macroporeux a base de nickel obtenu par comalaxage et ayant un diametre median macroporeux superieur a 300 nm et son utilisation en hydrogenation d'hydrocarbures
CN201580031619.1A CN106604978B (zh) 2014-06-13 2015-06-09 具有大于300纳米中值大孔直径的中孔和大孔共混镍活性相的催化剂及其在氢化中的用途
RU2017100932A RU2683776C2 (ru) 2014-06-13 2015-06-09 Мезопористый и макропористый катализатор на основе никеля, полученный совместным пластицированием и имеющий медианный диаметр макропор, превышающий 300 нм, и его применение при гидрировании углеводородов
US15/318,611 US10258969B2 (en) 2014-06-13 2015-06-09 Catalyst with a mesoporous and macroporous co-mixed nickel active phase having a median macropore diameter of more than 300 nm, and its use in hydrogenation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR1455430A FR3022161B1 (fr) 2014-06-13 2014-06-13 Catalyseur a phase active de nickel comalaxee mesoporeux et macroporeux ayant un diametre median macroporeux superieur a 300 nm et son utilisation en hydrogenation

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FR3022161A1 FR3022161A1 (fr) 2015-12-18
FR3022161B1 true FR3022161B1 (fr) 2021-05-07

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FR3061037B1 (fr) * 2016-12-23 2021-07-02 Ifp Energies Now Solide porteur d'oxygene a base de tectosilicates, son procede de preparation et son utilisation pour un procede d'oxydo-reduction en boucle chimique
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US10655074B2 (en) 2017-02-12 2020-05-19 Mag{hacek over (e)}m{hacek over (a)} Technology LLC Multi-stage process and device for reducing environmental contaminates in heavy marine fuel oil
US12071592B2 (en) 2017-02-12 2024-08-27 Magēmā Technology LLC Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil
US10604709B2 (en) 2017-02-12 2020-03-31 Magēmā Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials
CN108786833B (zh) * 2017-05-02 2020-09-11 中国石油化工股份有限公司 一种重油加氢催化剂及其制备方法
FR3068982A1 (fr) * 2017-07-13 2019-01-18 IFP Energies Nouvelles Procede d'hydrogenation selective mettant en œuvre un catalyseur obtenu par comalaxage comprenant un support specifique
FR3068985A1 (fr) * 2017-07-13 2019-01-18 IFP Energies Nouvelles Procede d’hydrogenation des aromatiques mettant en oeuvre un catalyseur obtenu par comalaxage comprenant un support specifique
FR3068984B1 (fr) * 2017-07-13 2020-01-17 IFP Energies Nouvelles Procede d'hydrogenation des aromatiques mettant en œuvre un catalyseur obtenu par impregnation comprenant un support specifique.
FR3076746B1 (fr) * 2018-01-15 2022-07-01 Ifp Energies Now Procede de preparation d'un catalyseur particulier d'hydrogenation selective par malaxage et impregnation
FR3076747B1 (fr) * 2018-01-15 2022-06-10 Ifp Energies Now Procede de preparation d'un catalyseur particulier d'hydrogenation selective et d'hydrogenation des aromatiques par malaxage
FR3080117B1 (fr) * 2018-04-11 2020-04-03 IFP Energies Nouvelles Procede de captation de l'arsenic mettant en œuvre une masse de captation a base de particules d'oxyde de nickel
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EP3154686A1 (fr) 2017-04-19
RU2017100932A3 (fr) 2018-12-14
WO2015189191A1 (fr) 2015-12-17
RU2017100932A (ru) 2018-07-16
CN106604978A (zh) 2017-04-26
US20170120224A1 (en) 2017-05-04
FR3022161A1 (fr) 2015-12-18
RU2683776C2 (ru) 2019-04-02
CN106604978B (zh) 2020-03-03

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