BRPI0605370A - processo de hidrogenação seletiva pelo uso de um catalisador sulfurado - Google Patents

processo de hidrogenação seletiva pelo uso de um catalisador sulfurado

Info

Publication number
BRPI0605370A
BRPI0605370A BRPI0605370-0A BRPI0605370A BRPI0605370A BR PI0605370 A BRPI0605370 A BR PI0605370A BR PI0605370 A BRPI0605370 A BR PI0605370A BR PI0605370 A BRPI0605370 A BR PI0605370A
Authority
BR
Brazil
Prior art keywords
compounds
catalyst
range
selective hydrogenation
hydrogenation process
Prior art date
Application number
BRPI0605370-0A
Other languages
English (en)
Inventor
Christophe Bouchy
Florent Picard
Nathalie Marchal-George
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 BRPI0605370A publication Critical patent/BRPI0605370A/pt
Publication of BRPI0605370B1 publication Critical patent/BRPI0605370B1/pt

Links

Classifications

    • 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
    • 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
    • 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
    • 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
    • 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
    • C10G45/06—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
    • 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
    • C10G45/32—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
    • C10G45/38—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with 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
    • 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

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

PROCESSO DE HIDROGENAçãO SELETIVA PELO USO DE UM CATALISADOR SULFURADO. A presente invenção refere-se a um processo para executar, juntamente, a hidrogenação de compostos poliinsaturados em compostos monoinsaturados contidos em gasolinas e para transformar compostos leves contendo enxofre em compostos mais pesados pela reação com compostos insaturados, o processo citado empregando um catalisador com suporte compreendendo, no mínimo, um metal do grupo VIB e, no mínimo, um metal não nobre do grupo VIII utilizado na forma sulfurizada depositada em um suporte e tendo uma composição específica. O processo da invenção consiste em colocar a alimentação em contato com o catalisador a uma temperatura na faixa de 80<198>C a 220<198>C a uma velocidade espacial horária de líquido na faixa de 1 h¬ -1¬ a 10 h¬ -1¬ e a uma pressão na faixa de 0,5 a 5 Mpa.
BRPI0605370A 2005-12-22 2006-12-22 processo de hidrogenação seletiva pelo uso de um catalisador sulfurado BRPI0605370B1 (pt)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR0513174A FR2895416B1 (fr) 2005-12-22 2005-12-22 Procede d'hydrogenation selective mettant en oeuvre un catalyseur sulfure

Publications (2)

Publication Number Publication Date
BRPI0605370A true BRPI0605370A (pt) 2007-10-16
BRPI0605370B1 BRPI0605370B1 (pt) 2016-05-03

Family

ID=37052593

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0605370A BRPI0605370B1 (pt) 2005-12-22 2006-12-22 processo de hidrogenação seletiva pelo uso de um catalisador sulfurado

Country Status (7)

Country Link
US (1) US7645376B2 (pt)
EP (1) EP1800748B1 (pt)
JP (1) JP5392979B2 (pt)
KR (1) KR101345523B1 (pt)
CN (1) CN101024779B (pt)
BR (1) BRPI0605370B1 (pt)
FR (1) FR2895416B1 (pt)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
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
FR2935389B1 (fr) * 2008-09-04 2012-05-11 Inst Francais Du Petrole Procede d'hydrogenation selective mettant en oeuvre un catalyseur sulfure de composition specifique
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
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
FR2990882B1 (fr) * 2012-05-24 2015-05-15 IFP Energies Nouvelles Procede de preparation d'un catalyseur a base d'un metal du groupe viii et contenant du silicium et procede d'hydrogenation selective mettant en oeuvre ledit catalyseur
FR2993570B1 (fr) * 2012-07-17 2015-12-04 IFP Energies Nouvelles Procede de production d'une essence legere basse teneur en soufre
FR2993569B1 (fr) * 2012-07-17 2015-12-04 IFP Energies Nouvelles Procede de desulfuration d'une essence
FR2997415B1 (fr) * 2012-10-29 2015-10-02 IFP Energies Nouvelles Procede de production d'une essence a basse teneur en soufre
US20150231611A1 (en) * 2014-02-19 2015-08-20 Uop Llc Methods and apparatuses for regenerating catalysts for hydrocarbon production
CN105478146B (zh) * 2014-10-09 2018-01-05 中国石油化工股份有限公司 加氢脱硫催化剂和体系及其制备方法和柴油的加氢脱硫方法
FR3035117B1 (fr) 2015-04-15 2019-04-19 IFP Energies Nouvelles Procede d'adoucissement en composes du type sulfure d'une essence olefinique
DE102015015152B4 (de) 2015-11-25 2017-07-20 Dräger Safety AG & Co. KGaA Verfahren zur Überprüfung eines Gassensors in einem Gasmesssystem
FR3049955B1 (fr) 2016-04-08 2018-04-06 IFP Energies Nouvelles Procede de traitement d'une essence
CN106179522B (zh) * 2016-07-08 2018-04-20 山东科技大学 一种加氢催化剂的器外预硫化方法
FR3057578B1 (fr) 2016-10-19 2018-11-16 IFP Energies Nouvelles Procede d'hydrodesulfuration d'une essence olefinique.
BR112019010168A2 (pt) 2016-11-23 2019-09-17 Haldor Topsøe A/S processo para dessulfurização de hidrocarbonetos
WO2018096064A1 (en) * 2016-11-23 2018-05-31 Haldor Topsøe A/S Process for desulfurization of hydrocarbons
CN106876710B (zh) * 2016-12-22 2020-03-24 湖南中科星城石墨有限公司 一种用于锂离子电池的软碳负极材料及其制备方法
EP3822332A1 (en) * 2019-11-13 2021-05-19 Indian Oil Corporation Limited Catalyst for selective hydrogenation of diolefins and method for preparing catalyst

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
OA02047A (fr) * 1965-02-13 1970-05-05 Inst Francais Du Petrole Procédé d'hydrogenation selective des diolefines.
GB1379202A (en) * 1970-11-30 1975-01-02 Shell Int Research Two-stage hydrocracking process employing a supported nickel- molybdenum catalyst
GB1415417A (en) * 1973-10-12 1975-11-26 American Cyanamid Co Hydrotreating of petroleum distillates using shaped catalyst prtticles
US4456703A (en) * 1982-05-07 1984-06-26 Exxon Research And Engineering Co. High surface area nickel aluminate spinel catalyst for steam reforming
FR2790000B1 (fr) * 1999-02-24 2001-04-13 Inst Francais Du Petrole Procede de production d'essences a faible teneur en soufre
FR2797639B1 (fr) * 1999-08-19 2001-09-21 Inst Francais Du Petrole Procede de production d'essences a faible teneur en soufre
US6231752B1 (en) * 1999-09-17 2001-05-15 Catalytic Distillation Technologies Process for the removal of mercaptans
DE10152842A1 (de) * 2001-10-25 2003-05-08 Oxeno Olefinchemie Gmbh Hydroisomerisierung von Olefinen mit 4-6 Kohlenstoffatomen
FR2837831B1 (fr) * 2002-03-29 2005-02-11 Inst Francais Du Petrole Procede de production d'hydrocarbures a faible teneur en soufre et en mercaptans
FR2840316B1 (fr) * 2002-06-03 2005-08-26 Inst Francais Du Petrole Procede d'hydrodesulfuration de coupes contenant des composes soufres et des olefines en presence d'un catalyseur comprenant un element du groupe viii et du tungstene
FR2840315B1 (fr) * 2002-06-03 2004-08-20 Inst Francais Du Petrole Procede d'hydrodesulfuration de coupes contenant des composes soufres et des olefines en presence d'un catalyseur supporte comprenant des metaux des groupes viii et vib
FR2850299B1 (fr) * 2003-01-29 2006-12-01 Inst Francais Du Petrole Catalyseurs partiellement cokes utilisables dans l'hydrotraitement des coupes contenant des composes soufres et des olefines

Also Published As

Publication number Publication date
FR2895416A1 (fr) 2007-06-29
FR2895416B1 (fr) 2011-08-26
US20070173674A1 (en) 2007-07-26
CN101024779B (zh) 2012-07-04
KR20070066984A (ko) 2007-06-27
EP1800748A3 (fr) 2011-04-20
EP1800748B1 (fr) 2016-04-27
JP5392979B2 (ja) 2014-01-22
EP1800748A2 (fr) 2007-06-27
BRPI0605370B1 (pt) 2016-05-03
US7645376B2 (en) 2010-01-12
CN101024779A (zh) 2007-08-29
JP2007177245A (ja) 2007-07-12
KR101345523B1 (ko) 2013-12-27

Similar Documents

Publication Publication Date Title
BRPI0605370A (pt) processo de hidrogenação seletiva pelo uso de um catalisador sulfurado
BRPI0605369A (pt) processo de hidrogenação seletiva que emprega um catalisador com um suporte especìfico
BRPI0605367A (pt) processo para hidrogenação seletiva de compostos poliinsaturados em compostos monoinsaturados
US8674151B2 (en) Two-step hydrotreatment of a feed derived from a renewable source using a first, metallic, catalyst and a second, sulphurized, catalyst
ES2567159T3 (es) Método para la deshidratación de alcoholes grasos
SG159489A1 (en) Selective hydrogenation process employing a sulphurized catalyst with a specific composition
BRPI0515129A (pt) processo para telomerização de olefinas não cìclicas
BRPI0414865A (pt) processo para ativação de um catalisador de hidrotratamento
AR063261A1 (es) Proceso para preparar un catalizador hidrotratamiento
BR0101856A (pt) Processo para craqueamento catalìtico de uma alimentação de hidrocarboneto
MY146965A (en) Process for the manufacture of diesel range hydrocarbons
TNSN07487A1 (en) Process for the manufacture of diesel range hydrocarbons
BR0317023A (pt) Processo para produção de álcool
BRPI0606185A2 (pt) catalisador de redução de enxofre na gasolina para processo de craqueamento catalìtico de fluido
PT1034841E (pt) Composicao catalitica para a melhoria de misturas de hidrocarbonetos
TW200628442A (en) Toluene disproportionation process utilizing mild sulfiding during startup
WO2001023087A8 (en) Hydrocarbon hydrogenation catalyst and process
AR073144A1 (es) Metodo para producir olefinas livianas en unidades de craqueo catalitico con deficiencia energetica
BR112018077429A2 (pt) preparação de um catalisador à base de zsm-5; uso no processo de desalquilação de etilbenzeno
AR020178A1 (es) Procedimiento para el enriquecimiento de hidrocarburos que hierven en el rango de las naftas, catalizador para tal procedimiento y procedimiento parapreparar dicho catalizador
BR0211897A (pt) Processo e aparelho para a produção de olefinas ramificadas, e, usos de catalisadores e similares, e das olefinas ramificadas
ES2055289T3 (es) Hidrogenacion con catalizadores de cu-al.
ES2532908T3 (es) Procedimiento para la eliminación de compuestos de azufre de materias primas de hidrocarburos
BR112015024541A2 (pt) processo de rejuvenescimento de um catalisador de hidrotratamento usado
BR112012006491A2 (pt) processo para a hidrogenação catalítica de um composto nitro aromático ou heteroaromático, e, catalisador de platina.

Legal Events

Date Code Title Description
B07A Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 22/12/2006, OBSERVADAS AS CONDICOES LEGAIS.

B21F Lapse acc. art. 78, item iv - on non-payment of the annual fees in time
B24J Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12)