CN101665720A - 利用具有规定组成的硫化催化剂的选择加氢方法 - Google Patents

利用具有规定组成的硫化催化剂的选择加氢方法 Download PDF

Info

Publication number
CN101665720A
CN101665720A CN200910170584A CN200910170584A CN101665720A CN 101665720 A CN101665720 A CN 101665720A CN 200910170584 A CN200910170584 A CN 200910170584A CN 200910170584 A CN200910170584 A CN 200910170584A CN 101665720 A CN101665720 A CN 101665720A
Authority
CN
China
Prior art keywords
catalyst
metal
weight
catalyzer
group viii
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.)
Pending
Application number
CN200910170584A
Other languages
English (en)
Chinese (zh)
Inventor
M·蒙蒂莱特
E·德弗斯
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 Co
Original Assignee
Ifp Co
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 Co filed Critical Ifp Co
Priority to CN201611087647.8A priority Critical patent/CN106867575A/zh
Publication of CN101665720A publication Critical patent/CN101665720A/zh
Pending legal-status Critical Current

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
    • 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
    • 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
    • B01J35/633—Pore volume less than 0.5 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
    • B01J35/63—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
    • B01J35/63—Pore volume
    • B01J35/638—Pore volume more than 1.0 ml/g
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
CN200910170584A 2008-09-04 2009-09-04 利用具有规定组成的硫化催化剂的选择加氢方法 Pending CN101665720A (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611087647.8A CN106867575A (zh) 2008-09-04 2009-09-04 利用具有规定组成的硫化催化剂的选择加氢方法

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0804842A FR2935389B1 (fr) 2008-09-04 2008-09-04 Procede d'hydrogenation selective mettant en oeuvre un catalyseur sulfure de composition specifique
FR08/04842 2008-09-04

Related Child Applications (1)

Application Number Title Priority Date Filing Date
CN201611087647.8A Division CN106867575A (zh) 2008-09-04 2009-09-04 利用具有规定组成的硫化催化剂的选择加氢方法

Publications (1)

Publication Number Publication Date
CN101665720A true CN101665720A (zh) 2010-03-10

Family

ID=40578636

Family Applications (2)

Application Number Title Priority Date Filing Date
CN200910170584A Pending CN101665720A (zh) 2008-09-04 2009-09-04 利用具有规定组成的硫化催化剂的选择加氢方法
CN201611087647.8A Pending CN106867575A (zh) 2008-09-04 2009-09-04 利用具有规定组成的硫化催化剂的选择加氢方法

Family Applications After (1)

Application Number Title Priority Date Filing Date
CN201611087647.8A Pending CN106867575A (zh) 2008-09-04 2009-09-04 利用具有规定组成的硫化催化剂的选择加氢方法

Country Status (9)

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

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103146420A (zh) * 2011-12-06 2013-06-12 中国石油天然气股份有限公司 一种汽油加氢处理的方法
CN103361110A (zh) * 2012-03-29 2013-10-23 Ifp新能源公司 汽油的选择性氢化方法
WO2014047753A1 (zh) * 2012-09-28 2014-04-03 中国石油天然气股份有限公司 一种使不饱和化合物选择加氢的方法
CN104755595A (zh) * 2012-10-29 2015-07-01 Ifp新能源公司 制备具有低硫含量的汽油的方法
CN115443187A (zh) * 2020-05-07 2022-12-06 Ifp 新能源公司 包含载体和特定镍钼比的加氢催化剂
CN115461145A (zh) * 2020-05-07 2022-12-09 Ifp 新能源公司 包含铝酸盐形式的特定载体的选择性加氢催化剂
CN115461144A (zh) * 2020-05-07 2022-12-09 Ifp 新能源公司 具有镍和钼的特定分布的选择性加氢催化剂

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2986799B1 (fr) 2012-02-15 2015-02-06 IFP Energies Nouvelles Procede de conversion d'une charge lourde, mettant en oeuvre une unite de craquage catalytique et une etape d'hydrogenation selective de l'essence issue du craquage catalytique
FR2993569B1 (fr) * 2012-07-17 2015-12-04 IFP Energies Nouvelles Procede de desulfuration d'une essence
FR3014896B1 (fr) 2013-12-18 2018-07-27 IFP Energies Nouvelles Procede d'hydrodesulfuration de coupes d'hydrocarbures
FR3030563B1 (fr) * 2014-12-18 2018-06-29 IFP Energies Nouvelles Procede d'adoucissement en composes du type sulfure d'une essence olefinique
FR3035117B1 (fr) 2015-04-15 2019-04-19 IFP Energies Nouvelles Procede d'adoucissement en composes du type sulfure d'une essence olefinique
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 (fr) 2016-04-08 2018-04-06 IFP Energies Nouvelles Procede de traitement d'une essence
FR3057578B1 (fr) 2016-10-19 2018-11-16 IFP Energies Nouvelles Procede d'hydrodesulfuration d'une essence olefinique.

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1314288A (en) * 1970-12-16 1973-04-18 Inst Francais Du Petrole Catalyst its preparation and its use in the hydrogenation of unsaturated hydrocarbons
CN1342102A (zh) * 1999-01-15 2002-03-27 阿克佐诺贝尔公司 新型混合金属催化剂、利用共沉淀的其制备及其用途
CN101024779A (zh) * 2005-12-22 2007-08-29 法国石油公司 使用硫化催化剂的选择性氢化方法
CN101214455A (zh) * 2007-12-27 2008-07-09 长沙矿冶研究院 一种负载型纳米加氢催化剂的制备方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2556235A1 (fr) * 1983-12-09 1985-06-14 Pro Catalyse Procede de fabrication d'un catalyseur a base d'alumine
FR2720754B1 (fr) 1994-06-01 1996-07-26 Inst Francais Du Petrole Procédé et installation pour le traitement par hydrogénation sélective d'une essence de craquage catalytique.
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
FR2797639B1 (fr) 1999-08-19 2001-09-21 Inst Francais Du Petrole Procede de production d'essences a faible teneur en soufre
US6469223B2 (en) 2000-01-04 2002-10-22 Fina Technology, Inc. Selective hydrogenation of dienes
FR2895414B1 (fr) * 2005-12-22 2011-07-29 Inst Francais Du Petrole Procede d'hydrogenation selective mettant en oeuvre un catalyseur presentant une porosite controlee
FR2895415B1 (fr) * 2005-12-22 2011-07-15 Inst Francais Du Petrole Procede d'hydrogenation selective mettant en oeuvre un catalyseur presentant un support specifique

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1314288A (en) * 1970-12-16 1973-04-18 Inst Francais Du Petrole Catalyst its preparation and its use in the hydrogenation of unsaturated hydrocarbons
CN1342102A (zh) * 1999-01-15 2002-03-27 阿克佐诺贝尔公司 新型混合金属催化剂、利用共沉淀的其制备及其用途
CN101024779A (zh) * 2005-12-22 2007-08-29 法国石油公司 使用硫化催化剂的选择性氢化方法
CN101214455A (zh) * 2007-12-27 2008-07-09 长沙矿冶研究院 一种负载型纳米加氢催化剂的制备方法

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9611435B2 (en) 2011-12-06 2017-04-04 Petrochina Company Limited Method for selective hydrogenation of unsaturated compound
CN103145516A (zh) * 2011-12-06 2013-06-12 中国石油天然气股份有限公司 一种使不饱和化合物选择加氢的方法
CN103146429A (zh) * 2011-12-06 2013-06-12 中国石油天然气股份有限公司 一种液化气加氢处理的方法
CN103146420A (zh) * 2011-12-06 2013-06-12 中国石油天然气股份有限公司 一种汽油加氢处理的方法
CN103145516B (zh) * 2011-12-06 2015-01-21 中国石油天然气股份有限公司 一种使不饱和化合物选择加氢的方法
CN103146429B (zh) * 2011-12-06 2015-08-19 中国石油天然气股份有限公司 一种液化气加氢处理的方法
CN103146420B (zh) * 2011-12-06 2015-11-18 中国石油天然气股份有限公司 一种汽油加氢处理的方法
US9422486B2 (en) 2011-12-06 2016-08-23 Petrochina Company Limited Selective hydrogenation catalyst for unsaturated compound
CN103361110A (zh) * 2012-03-29 2013-10-23 Ifp新能源公司 汽油的选择性氢化方法
CN103361110B (zh) * 2012-03-29 2017-05-17 Ifp新能源公司 汽油的选择性氢化方法
WO2014047753A1 (zh) * 2012-09-28 2014-04-03 中国石油天然气股份有限公司 一种使不饱和化合物选择加氢的方法
CN104755595A (zh) * 2012-10-29 2015-07-01 Ifp新能源公司 制备具有低硫含量的汽油的方法
CN104755595B (zh) * 2012-10-29 2018-10-23 Ifp 新能源公司 制备具有低硫含量的汽油的方法
CN115443187A (zh) * 2020-05-07 2022-12-06 Ifp 新能源公司 包含载体和特定镍钼比的加氢催化剂
CN115461145A (zh) * 2020-05-07 2022-12-09 Ifp 新能源公司 包含铝酸盐形式的特定载体的选择性加氢催化剂
CN115461144A (zh) * 2020-05-07 2022-12-09 Ifp 新能源公司 具有镍和钼的特定分布的选择性加氢催化剂
CN115443187B (zh) * 2020-05-07 2025-07-29 Ifp新能源公司 包含载体和特定镍钼比的加氢催化剂

Also Published As

Publication number Publication date
FR2935389A1 (fr) 2010-03-05
SG159489A1 (en) 2010-03-30
TW201016318A (en) 2010-05-01
JP5563259B2 (ja) 2014-07-30
DK2161076T3 (en) 2018-08-06
TWI492788B (zh) 2015-07-21
JP2010090366A (ja) 2010-04-22
EP2161076B1 (fr) 2018-04-25
FR2935389B1 (fr) 2012-05-11
BRPI0902949B1 (pt) 2022-09-20
EP2161076A1 (fr) 2010-03-10
KR101668481B1 (ko) 2016-10-21
CN106867575A (zh) 2017-06-20
BRPI0902949A2 (pt) 2010-06-01
KR20100028502A (ko) 2010-03-12

Similar Documents

Publication Publication Date Title
CN101665720A (zh) 利用具有规定组成的硫化催化剂的选择加氢方法
CN101024779B (zh) 使用硫化催化剂的选择性氢化方法
CN101445748B (zh) 用于含砷的烯烃汽油脱硫的两步法
JP6244094B2 (ja) ガソリンの選択的水素化方法
CN101205483B (zh) 使用有特定载体的催化剂的选择性氢化方法
CN101016479B (zh) 使用具有控制孔隙度的催化剂的选择性氢化方法
JP2025185083A (ja) ポリ不飽和化合物および軽質硫黄化合物を含むガソリンの選択的水素化のための方法
JP2023550821A (ja) メソ多孔性・マクロ多孔性担体上の触媒の存在下におけるガソリンの選択的水素化のための方法
CN103170343B (zh) 捕获砷并对催化裂化汽油选择性加氢脱硫的催化吸附剂
CN115461144B (zh) 具有镍和钼的特定分布的选择性加氢催化剂
CN115461145B (zh) 包含铝酸盐形式的特定载体的选择性加氢催化剂
CN118146843B (zh) 一种液化石油气深度脱硫方法

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
CB02 Change of applicant information

Address after: France Ruez - Ma Maison

Applicant after: IFP Energies Nouvelles

Address before: France Ruez - Ma Maison

Applicant before: Ifp En Nouvelles

COR Change of bibliographic data
RJ01 Rejection of invention patent application after publication

Application publication date: 20100310

RJ01 Rejection of invention patent application after publication