BR9713345A - Catalisador contendo fósforo e processo de hidrotratamento de cargas petrolìferas com esse catalisador. - Google Patents

Catalisador contendo fósforo e processo de hidrotratamento de cargas petrolìferas com esse catalisador.

Info

Publication number
BR9713345A
BR9713345A BR9713345-0A BR9713345A BR9713345A BR 9713345 A BR9713345 A BR 9713345A BR 9713345 A BR9713345 A BR 9713345A BR 9713345 A BR9713345 A BR 9713345A
Authority
BR
Brazil
Prior art keywords
catalyst
phosphorus
diameter
pores
oxide
Prior art date
Application number
BR9713345-0A
Other languages
English (en)
Inventor
Samuel Mignard
Nathalie George-Marchal
Virginie Harle
Slavik Kasztelan
Original Assignee
Inst Francais Du Petrole Orgao
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=9497550&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=BR9713345(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Inst Francais Du Petrole Orgao filed Critical Inst Francais Du Petrole Orgao
Publication of BR9713345A publication Critical patent/BR9713345A/pt

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G49/00Treatment 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
    • C10G49/02Treatment 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
    • C10G49/04Treatment 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J35/615
    • B01J35/647
    • B01J35/66
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining 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
    • C10G45/04Refining 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
    • C10G45/06Refining 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
    • C10G45/08Refining 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

Abstract

Patente de Invenção:<B>"CATALISADOR CONTENDO FóSFORO E PROCESSO DE HIDROTRATAMENTO DE CARGAS PETROLìFERAS COM ESSE CATALISADOR"<D>. A invenção refere-se a um catalisador à base de alumina que contém, expressos em teores ponderais em óxidos, de 2 a 10% em peso de óxido de cobalto CoO, de 10 a 30% em peso de óxido de molibdênio MoO3 e de 4 a 10% de óxido de fósforo P2 O5, que apresenta uma superfície BET compreendida entre 100 e 300 m^ 2^/g, uma compressão ESH superior a 1,4 MPa, um diâmetro médio de poros compreendido entre 8 a 11 nm, o volume poroso dos poros de diâmetro superior a 14 nm é inferior a 0,08 ml/g, o volume dos poros de diâmetro inferior a 8nm, no máximo igual a 0,05 ml/g, o volume dos poros de diâmetro compreendido entre 8 e 14nm está compreendido entre 0,20 ml/g e 0,8 ml/g. A invenção refere-se igualmente a um processo de hidrotratamento com esse catalisador, e, em particular, de hidrodessulfuração.
BR9713345-0A 1996-11-13 1997-11-07 Catalisador contendo fósforo e processo de hidrotratamento de cargas petrolìferas com esse catalisador. BR9713345A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9613797A FR2755625B1 (fr) 1996-11-13 1996-11-13 Catalyseur contenant du phosphore et procede d'hydrotraitement de charges petrolieres avec ce catalyseur
PCT/FR1997/002006 WO1998020969A1 (fr) 1996-11-13 1997-11-07 Catalyseur contenant du phosphore et procede d'hydrotraitement de charges petrolieres avec ce catalyseur

Publications (1)

Publication Number Publication Date
BR9713345A true BR9713345A (pt) 2000-05-09

Family

ID=9497550

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9713345-0A BR9713345A (pt) 1996-11-13 1997-11-07 Catalisador contendo fósforo e processo de hidrotratamento de cargas petrolìferas com esse catalisador.

Country Status (14)

Country Link
EP (1) EP0952888B1 (pt)
JP (1) JP2001503328A (pt)
KR (1) KR100473668B1 (pt)
CN (1) CN1108190C (pt)
AT (1) ATE249276T1 (pt)
AU (1) AU731209B2 (pt)
BR (1) BR9713345A (pt)
CA (1) CA2270590A1 (pt)
DE (1) DE69724820T2 (pt)
DK (1) DK0952888T3 (pt)
FR (1) FR2755625B1 (pt)
NZ (1) NZ335179A (pt)
RU (1) RU2192923C2 (pt)
WO (1) WO1998020969A1 (pt)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101428213B (zh) * 2007-11-07 2011-04-20 中国科学院大连化学物理研究所 炭载类贵金属催化剂在纤维素加氢水解反应中的应用
CN101428214B (zh) * 2007-11-07 2011-01-19 中国科学院大连化学物理研究所 氧化铝负载类贵金属催化剂在纤维素加氢水解中的应用
FR2998488B1 (fr) * 2012-11-29 2015-02-06 Ifp Energies Now Catalyseur d hydrotraitement a partir d alumine gel et methode de preparation d un tel catalyseur
FR3022156B1 (fr) * 2014-06-13 2018-02-23 Ifp Energies Now Catalyseur mesoporeux et macroporeux a phase active comalaxee, son procede de preparation et son utilisation en hydrotraitement de residus
RU2616601C1 (ru) * 2016-03-10 2017-04-18 Открытое акционерное общество "Нефтяная компания "Роснефть" Катализатор гидрооблагораживания вакуумного газойля и способы его приготовления (варианты)
RU2620267C1 (ru) * 2016-03-17 2017-05-24 Открытое акционерное общество "Нефтяная компания "Роснефть" Катализатор гидрооблагораживания вакуумного газойля и способ его приготовления
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
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
US20190233741A1 (en) 2017-02-12 2019-08-01 Mag&#275;m&#257; Technology, LLC Multi-Stage Process and Device for Reducing Environmental Contaminates in Heavy Marine Fuel Oil
RU2712446C1 (ru) * 2019-07-30 2020-01-29 Акционерное общество "Специальное конструкторско-технологическое бюро "Катализатор" Способ приготовления носителя для катализаторов на основе оксида алюминия

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4752376A (en) * 1985-09-25 1988-06-21 Intevep, S.A. Multiple stepped process for the demetallization and desulfuration of heavy oil feedstocks
US4941964A (en) * 1988-03-14 1990-07-17 Texaco Inc. Hydrotreatment process employing catalyst with specified pore size distribution
JPH01270945A (ja) * 1988-04-21 1989-10-30 Sumitomo Metal Mining Co Ltd 炭化水素の水素化処理用触媒
US4940530A (en) * 1989-02-21 1990-07-10 Amoco Corporation Two-stage hydrocarbon conversion process
DE69119320T2 (de) * 1990-08-03 1996-11-07 Akzo Nobel Nv Verfahren zur hydrierende Entschwefelung
EP0526988A3 (en) * 1991-07-10 1993-03-31 Texaco Development Corporation Hydrotreatment process employing a mono-modal catalyst with specified pore size distribution
US5397456A (en) * 1993-02-19 1995-03-14 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution

Also Published As

Publication number Publication date
AU731209B2 (en) 2001-03-29
CN1108190C (zh) 2003-05-14
CA2270590A1 (fr) 1998-05-22
ATE249276T1 (de) 2003-09-15
WO1998020969A1 (fr) 1998-05-22
EP0952888B1 (fr) 2003-09-10
NZ335179A (en) 2000-12-22
FR2755625B1 (fr) 1998-12-11
CN1237919A (zh) 1999-12-08
AU5058598A (en) 1998-06-03
DE69724820D1 (de) 2003-10-16
KR20000053177A (ko) 2000-08-25
KR100473668B1 (ko) 2005-03-07
RU2192923C2 (ru) 2002-11-20
DK0952888T3 (da) 2004-01-05
EP0952888A1 (fr) 1999-11-03
FR2755625A1 (fr) 1998-05-15
DE69724820T2 (de) 2004-04-08
JP2001503328A (ja) 2001-03-13

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Legal Events

Date Code Title Description
B07A Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]
B09B Patent application refused [chapter 9.2 patent gazette]