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 PDFInfo
- 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
- Authority
- FR
- France
- Prior art keywords
- macroporeous
- active phase
- nickel
- catalyst
- comalaxed
- Prior art date
- Legal status (The legal status 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 status listed.)
- Active
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- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title abstract 8
- 239000003054 catalyst Substances 0.000 title abstract 5
- 229910052759 nickel Inorganic materials 0.000 title abstract 4
- 238000005984 hydrogenation reaction Methods 0.000 title abstract 2
- 239000011159 matrix material Substances 0.000 abstract 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 abstract 2
- 229910052753 mercury Inorganic materials 0.000 abstract 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 abstract 2
- 238000002459 porosimetry Methods 0.000 abstract 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 229910052751 metal Inorganic materials 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 239000011148 porous material Substances 0.000 abstract 1
Classifications
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- 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
- C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds
- C10G45/34—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
- C10G45/36—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
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- 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
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J33/00—Protection of catalysts, e.g. by coating
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/391—Physical properties of the active metal ingredient
- B01J35/393—Metal or metal oxide crystallite size
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- B01J35/613—10-100 m2/g
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- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
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- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/633—Pore volume less than 0.5 ml/g
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- 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
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- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
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- B01J35/643—Pore diameter less than 2 nm
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- B01J35/647—2-50 nm
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- B01J37/009—Preparation by separation, e.g. by filtration, decantation, screening
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- B01J37/02—Impregnation, coating or precipitation
- B01J37/0236—Drying, e.g. preparing a suspension, adding a soluble salt and drying
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- B01J37/036—Precipitation; Co-precipitation to form a gel or a cogel
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- B01J37/20—Sulfiding
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/03—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/03—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
- C07C5/05—Partial hydrogenation
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- C—CHEMISTRY; METALLURGY
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- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/10—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of aromatic six-membered rings
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- 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
- C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds
- C10G45/34—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
- C10G45/40—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing platinum group metals or compounds thereof
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- 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
- C10G45/44—Hydrogenation of the aromatic hydrocarbons
- C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
- C10G45/48—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
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- 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
- C10G45/44—Hydrogenation of the aromatic hydrocarbons
- C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
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- B01J2235/15—X-ray diffraction
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
- C07C2521/04—Alumina
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
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- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/14—The ring being saturated
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- 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
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- C10G2300/1096—Aromatics or polyaromatics
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- 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
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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.
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 |
Publications (2)
Publication Number | Publication Date |
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FR3022161A1 FR3022161A1 (fr) | 2015-12-18 |
FR3022161B1 true FR3022161B1 (fr) | 2021-05-07 |
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FR1455430A Active 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 |
Country Status (6)
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US (1) | US10258969B2 (fr) |
EP (1) | EP3154686A1 (fr) |
CN (1) | CN106604978B (fr) |
FR (1) | FR3022161B1 (fr) |
RU (1) | RU2683776C2 (fr) |
WO (1) | WO2015189191A1 (fr) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3025728B1 (fr) * | 2014-09-11 | 2018-04-20 | IFP Energies Nouvelles | Catalyseur mesoporeux a base de nickel et son utilisation en hydrogenation. |
FR3061036B1 (fr) | 2016-12-23 | 2021-07-02 | Ifp Energies Now | Solide porteur d'oxygene macroporeux a matrice ceramique d'oxydes, son procede de preparation et son utilisation pour un procede d'oxydo-reduction en boucle chimique |
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 |
US12025435B2 (en) | 2017-02-12 | 2024-07-02 | Magēmã Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil |
US11788017B2 (en) | 2017-02-12 | 2023-10-17 | Magëmã Technology LLC | Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil |
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 |
FR3083992B1 (fr) * | 2018-07-23 | 2020-07-24 | Ifp Energies Now | Catalyseur comalaxe issu de solutions a base d'heteropolyanions, son procede de preparation et son utilisation en hydroconversion de charges hydrocarbonees lourdes |
FR3099388B1 (fr) * | 2019-07-31 | 2021-07-16 | Ifp Energies Now | Catalyseur comprenant une phase active de nickel sous forme de petites particules repartie en croute et un alliage nickel cuivre |
CN112717940B (zh) * | 2019-10-28 | 2023-07-21 | 中国石油化工股份有限公司 | 用于制γ-丁内酯的催化剂及其制备方法和应用 |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
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US4301037A (en) * | 1980-04-01 | 1981-11-17 | W. R. Grace & Co. | Extruded alumina catalyst support having controlled distribution of pore sizes |
NL190750C (nl) * | 1984-06-21 | 1994-08-01 | Unilever Nv | Nikkelaluminaat katalysator, de bereiding daarvan en het hydrogeneren van onverzadigde organische verbindingen daarmee. |
CA1319359C (fr) * | 1987-05-08 | 1993-06-22 | Wilhelmus P. Van Beek | Catalyseur d'hydrogenation |
DE4310971A1 (de) * | 1993-04-03 | 1994-10-06 | Huels Chemische Werke Ag | Nickel/Aluminiumoxid-Katalysator, Verfahren zu seiner Herstellung, seine Verwendung sowie Verfahren zur Hydrierung von aromatischen Kohlenwasserstoffen mit Hilfe des Katalysators |
WO1997032817A1 (fr) * | 1996-03-05 | 1997-09-12 | Goro Sato | Sol d'alumine, son procede de preparation, procede de preparation d'un moulage d'alumine l'utilisant, et catalyseur a base d'alumine ainsi prepare |
DE60037136D1 (de) * | 1999-12-21 | 2007-12-27 | Grace W R & Co | Aus aluminiumtrihydrat hergestellte aluminiumoxid-verbundstoffe mit hohem porenvolumen und hoher spezifischer oberfläche, deren herstellung und verwendung |
US6589908B1 (en) * | 2000-11-28 | 2003-07-08 | Shell Oil Company | Method of making alumina having bimodal pore structure, and catalysts made therefrom |
US7790652B2 (en) | 2003-09-17 | 2010-09-07 | Shell Oil Company | Process and catalyst for the hydroconversion of a heavy hydrocarbon feedstock |
KR20100076955A (ko) * | 2007-08-27 | 2010-07-06 | 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 | 무정형 실리카-알루미나 조성물 및 이 조성물의 제조 및 사용 방법 |
-
2014
- 2014-06-13 FR FR1455430A patent/FR3022161B1/fr active Active
-
2015
- 2015-06-09 EP EP15730988.1A patent/EP3154686A1/fr not_active Withdrawn
- 2015-06-09 WO PCT/EP2015/062817 patent/WO2015189191A1/fr active Application Filing
- 2015-06-09 CN CN201580031619.1A patent/CN106604978B/zh active Active
- 2015-06-09 RU RU2017100932A patent/RU2683776C2/ru not_active IP Right Cessation
- 2015-06-09 US US15/318,611 patent/US10258969B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
US10258969B2 (en) | 2019-04-16 |
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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