SG159489A1 - Selective hydrogenation process employing a sulphurized catalyst with a specific composition - Google Patents

Selective hydrogenation process employing a sulphurized catalyst with a specific composition

Info

Publication number
SG159489A1
SG159489A1 SG200905864-5A SG2009058645A SG159489A1 SG 159489 A1 SG159489 A1 SG 159489A1 SG 2009058645 A SG2009058645 A SG 2009058645A SG 159489 A1 SG159489 A1 SG 159489A1
Authority
SG
Singapore
Prior art keywords
catalyst
metal
specific composition
selective hydrogenation
process employing
Prior art date
Application number
SG200905864-5A
Inventor
Maxime Montillet
Elodie Devers
Original Assignee
Inst Francais Du Petrole
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 Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Publication of SG159489A1 publication Critical patent/SG159489A1/en

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
    • 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
    • C10G45/06—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 nickel or cobalt metal, or compounds thereof
    • C10G45/08—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 nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • C10G45/06—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 nickel or cobalt metal, 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
    • 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
    • B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24—Chromium, molybdenum or tungsten
    • 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
    • B01J23/74—Iron group metals
    • 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
    • B01J35/30—
    • 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
    • B01J37/20—Sulfiding
    • 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
    • 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
    • B01J35/615—
    • B01J35/633—
    • B01J35/635—
    • B01J35/638—
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/104—Light gasoline having a boiling range of about 20 - 100 °C
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • 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
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV
    • 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
    • C10G2300/70—Catalyst aspects
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline

Abstract

The invention concerns a process for carrying out joint selective hydrogenation of polyunsaturated compounds into mono-unsaturated compounds contained in gasolines, as well as weighting light sulphur-containing compounds by reaction with unsaturated compounds, said process employing a supported catalyst comprising at least one metal from group VIb and at least one non-noble metal from group VIII used in the sulphurized form deposited on a support. The catalyst has a specific composition, an optimized ratio of group VIb metal to group VIII metal and an optimized density of the element from group VIb per unit surface area of catalyst.
SG200905864-5A 2008-09-04 2009-09-03 Selective hydrogenation process employing a sulphurized catalyst with a specific composition SG159489A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR0804842A FR2935389B1 (en) 2008-09-04 2008-09-04 SELECTIVE HYDROGENATION PROCESS USING SULFIDE CATALYST OF SPECIFIC COMPOSITION

Publications (1)

Publication Number Publication Date
SG159489A1 true SG159489A1 (en) 2010-03-30

Family

ID=40578636

Family Applications (1)

Application Number Title Priority Date Filing Date
SG200905864-5A SG159489A1 (en) 2008-09-04 2009-09-03 Selective hydrogenation process employing a sulphurized catalyst with a specific composition

Country Status (9)

Country Link
EP (1) EP2161076B1 (en)
JP (1) JP5563259B2 (en)
KR (1) KR101668481B1 (en)
CN (2) CN101665720A (en)
BR (1) BRPI0902949B1 (en)
DK (1) DK2161076T3 (en)
FR (1) FR2935389B1 (en)
SG (1) SG159489A1 (en)
TW (1) TWI492788B (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103143366B (en) 2011-12-06 2015-05-13 中国石油天然气股份有限公司 Selective hydrogenation catalyst for unsaturated compound
WO2014047753A1 (en) * 2012-09-28 2014-04-03 中国石油天然气股份有限公司 Method for selective hydrogenation of unsaturated compound
FR2986799B1 (en) 2012-02-15 2015-02-06 IFP Energies Nouvelles HEAVY LOAD CONVERTING METHOD USING CATALYTIC CRACKING UNIT AND SELECTIVE HYDROGENATION STEP FROM CATALYTIC CRACKING GASOLINE
FR2988732B1 (en) * 2012-03-29 2015-02-06 IFP Energies Nouvelles METHOD FOR SELECTIVELY HYDROGENATING A GASOLINE
FR2993569B1 (en) * 2012-07-17 2015-12-04 IFP Energies Nouvelles METHOD OF DESULFURIZING A GASOLINE
FR2997415B1 (en) * 2012-10-29 2015-10-02 IFP Energies Nouvelles PROCESS FOR PRODUCING LOW SULFUR CONTENT GASOLINE
FR3014896B1 (en) 2013-12-18 2018-07-27 IFP Energies Nouvelles PROCESS FOR HYDRODESULFURIZATION OF HYDROCARBON CUT
FR3030563B1 (en) * 2014-12-18 2018-06-29 IFP Energies Nouvelles PROCESS FOR SOFTENING OF SULFIDE COMPOUNDS OF AN OLEFINIC ESSENCE
FR3035117B1 (en) 2015-04-15 2019-04-19 IFP Energies Nouvelles PROCESS FOR SOFTENING OF SULFIDE COMPOUNDS OF AN OLEFINIC ESSENCE
US9828093B2 (en) * 2015-05-27 2017-11-28 First Principles, Inc. System for recharging remotely controlled aerial vehicle, charging station and rechargeable remotely controlled aerial vehicle, and method of use thereof
US9714012B1 (en) 2016-01-22 2017-07-25 International Business Machines Corporation Power source element replacement during vehicle operation
FR3049955B1 (en) 2016-04-08 2018-04-06 IFP Energies Nouvelles PROCESS FOR TREATING A GASOLINE
FR3057578B1 (en) 2016-10-19 2018-11-16 IFP Energies Nouvelles PROCESS FOR HYDRODESULFURING OLEFINIC ESSENCE
FR3109897B1 (en) 2020-05-07 2023-11-24 Ifp Energies Now Selective hydrogenation catalyst comprising a specific support partly in aluminate form
FR3109899B1 (en) 2020-05-07 2023-11-24 Ifp Energies Now Hydrogenation catalyst comprising a support and a specific NiMo ratio

Family Cites Families (13)

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FR2118309A5 (en) * 1970-12-16 1972-07-28 Inst Francais Du Petrole
FR2556235A1 (en) * 1983-12-09 1985-06-14 Pro Catalyse METHOD FOR MANUFACTURING AN ALUMINA BASED CATALYST
FR2720754B1 (en) 1994-06-01 1996-07-26 Inst Francais Du Petrole Method and installation for the treatment by selective hydrogenation of a catalytic cracked gasoline.
ZA956008B (en) * 1994-07-21 1996-02-22 Shell Int Research Catalyst use thereof and process for preparation thereof
US5807477A (en) 1996-09-23 1998-09-15 Catalytic Distillation Technologies Process for the treatment of light naphtha hydrocarbon streams
US5851383A (en) * 1997-01-09 1998-12-22 Uop Llc Process for thioetherification and selective hydrogenation of light olefins
EP1150769B1 (en) * 1999-01-15 2007-06-20 Albemarle Netherlands B.V. A novel mixed metal catalyst, its preparation by co-precipitation, and its use
FR2797639B1 (en) 1999-08-19 2001-09-21 Inst Francais Du Petrole PROCESS FOR PRODUCING LOW SULFUR ESSENCE
US6469223B2 (en) 2000-01-04 2002-10-22 Fina Technology, Inc. Selective hydrogenation of dienes
FR2895414B1 (en) * 2005-12-22 2011-07-29 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS USING A CATALYST HAVING CONTROLLED POROSITY
FR2895416B1 (en) * 2005-12-22 2011-08-26 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS USING A SULFIDE CATALYST
FR2895415B1 (en) 2005-12-22 2011-07-15 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS USING A CATALYST HAVING A SPECIFIC SUPPORT
CN101214455A (en) * 2007-12-27 2008-07-09 长沙矿冶研究院 Preparation method of supported nano hydrogenation catalyst

Also Published As

Publication number Publication date
JP2010090366A (en) 2010-04-22
BRPI0902949A2 (en) 2010-06-01
DK2161076T3 (en) 2018-08-06
BRPI0902949B1 (en) 2022-09-20
CN106867575A (en) 2017-06-20
EP2161076B1 (en) 2018-04-25
TW201016318A (en) 2010-05-01
KR20100028502A (en) 2010-03-12
TWI492788B (en) 2015-07-21
FR2935389B1 (en) 2012-05-11
CN101665720A (en) 2010-03-10
FR2935389A1 (en) 2010-03-05
JP5563259B2 (en) 2014-07-30
EP2161076A1 (en) 2010-03-10
KR101668481B1 (en) 2016-10-21

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