FR3104463B1 - HYDROGENOLYSIS CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE - Google Patents

HYDROGENOLYSIS CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE Download PDF

Info

Publication number
FR3104463B1
FR3104463B1 FR1914609A FR1914609A FR3104463B1 FR 3104463 B1 FR3104463 B1 FR 3104463B1 FR 1914609 A FR1914609 A FR 1914609A FR 1914609 A FR1914609 A FR 1914609A FR 3104463 B1 FR3104463 B1 FR 3104463B1
Authority
FR
France
Prior art keywords
organic additive
catalyst obtained
hydrogenolysis catalyst
molten salts
brought
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
Application number
FR1914609A
Other languages
French (fr)
Other versions
FR3104463A1 (en
Inventor
Vincent Coupard
Malika Boualleg
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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 IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Priority to FR1914609A priority Critical patent/FR3104463B1/en
Publication of FR3104463A1 publication Critical patent/FR3104463A1/en
Application granted granted Critical
Publication of FR3104463B1 publication Critical patent/FR3104463B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
    • C10G49/04—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing nickel, cobalt, chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • 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
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85—Chromium, molybdenum or tungsten
    • B01J23/88—Molybdenum
    • B01J23/883—Molybdenum and nickel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Catalysts (AREA)

Abstract

Catalyseur d’hydrogénolyse susceptible d’être obtenu par le procédé comprenant au moins les étapes suivantes :a) on met en contact le support d’alumine avec au moins un additif organique ;b) on met en contact le support d’alumine avec au moins un sel métallique de nickel et au moins un sel métallique de molybdène ;c) on chauffe sous agitation le mélange solide obtenu à l’issue des étapes a) et b) ;d) on sèche le précurseur de catalyseur à l’issue de l’étape c) ;e) on réalise une étape de traitement thermique du précurseur de catalyseur séché obtenu à l’issue de l’étape d).Hydrogenolysis catalyst obtainable by the process comprising at least the following steps: a) the alumina support is brought into contact with at least one organic additive; b) the alumina support is brought into contact with at least one minus one metal salt of nickel and at least one metal salt of molybdenum; c) the solid mixture obtained at the end of stages a) and b) is heated with stirring; d) the catalyst precursor is dried at the end of step c); e) a step of heat treatment of the dried catalyst precursor obtained at the end of step d) is carried out.

FR1914609A 2019-12-17 2019-12-17 HYDROGENOLYSIS CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE Active FR3104463B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FR1914609A FR3104463B1 (en) 2019-12-17 2019-12-17 HYDROGENOLYSIS CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1914609A FR3104463B1 (en) 2019-12-17 2019-12-17 HYDROGENOLYSIS CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE
FR1914609 2019-12-17

Publications (2)

Publication Number Publication Date
FR3104463A1 FR3104463A1 (en) 2021-06-18
FR3104463B1 true FR3104463B1 (en) 2021-12-17

Family

ID=70228156

Family Applications (1)

Application Number Title Priority Date Filing Date
FR1914609A Active FR3104463B1 (en) 2019-12-17 2019-12-17 HYDROGENOLYSIS CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE

Country Status (1)

Country Link
FR (1) FR3104463B1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3090414B1 (en) * 2018-12-19 2022-07-29 Ifp Energies Now Selective catalyst in hydrogenolysis of ethyl-aromatics by conservation of methyl-aromatics.

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB191227955A (en) 1912-12-04 1913-11-13 James Yate Johnson Improvements in, or connected with, the Manufacture of Hydrogen.
US4177219A (en) 1978-04-24 1979-12-04 Standard Oil Company (Indiana) Process for selective ethyl scission of ethylaromatics to methylaromatics
US5036032A (en) 1988-03-25 1991-07-30 Exxon Research And Engineering Company Selective catalysts and their preparation for catalytic hydrocarbon synthesis
WO2002020702A1 (en) * 2000-09-04 2002-03-14 Akzo Nobel N.V. Process for effecting ultra-deep hds of hydrocarbon feedstocks
FR3018702B1 (en) 2014-03-20 2017-10-20 Ifp Energies Now FISCHER-TROPSCH CATALYST BASED ON A GROUP VIIIB METAL AND AN OXIDE SUPPORT COMPRISING ALUMINA, SILICA, SPINELLE AND PHOSPHORUS
FR3023184B1 (en) * 2014-07-04 2019-12-27 IFP Energies Nouvelles HIGH MOLYBDEN DENSITY HYDROTREATMENT CATALYST AND PREPARATION METHOD.
KR101634946B1 (en) * 2015-06-30 2016-07-01 한국에너지기술연구원 Methane steam reforming, using nickel/alumina nanocomposite catalyst or nickel/silica-alumina hybrid nanocomposite catalyst
FR3076747B1 (en) * 2018-01-15 2022-06-10 Ifp Energies Now METHOD FOR PREPARING A PARTICULAR CATALYST FOR SELECTIVE HYDROGENATION AND HYDROGENATION OF AROMATICS BY MIXING

Also Published As

Publication number Publication date
FR3104463A1 (en) 2021-06-18

Similar Documents

Publication Publication Date Title
FR3104463B1 (en) HYDROGENOLYSIS CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE
JP2018526389A5 (en)
JPWO2019208643A5 (en)
FR3104461B1 (en) SELECTIVE HYDROGENATION CATALYST OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE
Kong et al. Stainless steel-initiated thiosulfonylations of unactivated alkenes under solvent-free conditions in a mixer mill
US2394516A (en) Manufacture of amines
Zele et al. Photochemical synthesis of aroylated heterocycles under catalyst and additive free conditions
US2390470A (en) Preparation of alpha, beta-dichloropropionitrile
FR3104462B1 (en) CATALYST FOR THE HYDROGENATION OF AROMATIC COMPOUNDS OBTAINED FROM MOLTEN SALTS AND AN ORGANIC ADDITIVE
FR3089134B1 (en) A method of preparing an electrode catalytic material for electrochemical reduction reactions prepared by electroreduction.
TW201733676A (en) Cracking catalyst of 1,2-dichloroethane, method of producing the same and application thereof
Liu et al. Cu-mediated nitrogen atom transfer via C [triple bond, length as m-dash] N bond cleavage
CN110818603B (en) Preparation method of methomyl oxime
Wang et al. Cyanation of aromatic/vinylic boronic acids with α-cyanoacetates
FR3069460B3 (en) PROCESS FOR PREPARING A CATALYST BASED ON HIERARCHICAL ZEOLITE FOR THE FLAVORING OF C5 TO C9 ALKANES
BR112015028331B1 (en) improved method for preparing certain oximes and oxime ethers
Li et al. Hydrocyanation of Unsaturated Imines Using Potassium Hexacyanoferrate (II) as a Cyanide Source
FR3087787B1 (en) HYDROGENATION PROCESS INCLUDING A CATALYST PREPARED BY ADDITION OF AN ORGANIC COMPOUND IN GASEOUS PHASE
WO2014087431A1 (en) One pot process for the conversion of aroyl chlorides to acyl thioureas
US2729670A (en) Manufacture of acrylonitrile
Itoh et al. A Convenient Synthetic Method of Isoxazole Derivatives Using Copper (II) Nitrate
FR3043687B1 (en) SOL-GEL PROCESS FOR THE SYNTHESIS OF A LUMINESCENT MATERIAL OF GENERAL FORMULATION AXBYFZ: MN
CN104211600A (en) Preparation method of 3,5-binitro-o-methylbenzoyl chloride as liquid-state dinitolmide intermediate
Patil et al. Effective And Facile Synthesis Of Nitriles From Aldoximes By Using SnCl4
GB712745A (en) Improvements in or relating to the preparation of derivatives of organic amines

Legal Events

Date Code Title Description
PLFP Fee payment

Year of fee payment: 2

PLSC Publication of the preliminary search report

Effective date: 20210618

PLFP Fee payment

Year of fee payment: 3

PLFP Fee payment

Year of fee payment: 4

PLFP Fee payment

Year of fee payment: 5