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AU5058598A - Catalyst containing phosphorous and a process for hydrotreatment of petroleum feeds using the catalyst - Google Patents

Catalyst containing phosphorous and a process for hydrotreatment of petroleum feeds using the catalyst

Info

Publication number
AU5058598A
AU5058598A AU50585/98A AU5058598A AU5058598A AU 5058598 A AU5058598 A AU 5058598A AU 50585/98 A AU50585/98 A AU 50585/98A AU 5058598 A AU5058598 A AU 5058598A AU 5058598 A AU5058598 A AU 5058598A
Authority
AU
Australia
Prior art keywords
catalyst
pores
diameter
volume
hydrotreatment
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.)
Granted
Application number
AU50585/98A
Other versions
AU731209B2 (en
Inventor
Nathalie George-Marchal
Virginie Harle
Slavik Kasztelan
Samuel Mignard
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
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=AU5058598(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of AU5058598A publication Critical patent/AU5058598A/en
Application granted granted Critical
Publication of AU731209B2 publication Critical patent/AU731209B2/en
Anticipated expiration legal-status Critical
Ceased 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
    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • 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
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/66—Pore distribution
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

The invention concerns an alumina based catalyst containing, expressed in weight contents of oxides, 2-10 wt.% of cobalt oxide CoO, 10-30 wt.% of molybdenum oxide MoO3 and 4-10 wt.% of phosphorus oxide P2O5, having a BET surface between 100-300 m<2>/g, an ESH compression set higher than 1.4 MPa, an average pore diameter between 8-11 nm, the porous volume of pores of diameter greater than 14 nm is less than 0.08 ml/g, the volume of pores of diameter less than 8 nm not more than 0.05 ml/g,the volume of pores of diameter between 8 and 14 nm is between 0.20 ml/g and 0.8 ml/g. The invention also concerns a hydro-treating method using this catalyst, and in particular of hydrodesulphuration.
AU50585/98A 1996-11-13 1997-11-07 Catalyst containing phosphorous and a process for hydrotreatment of petroleum feeds using the catalyst Ceased AU731209B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR96/13797 1996-11-13
FR9613797A FR2755625B1 (en) 1996-11-13 1996-11-13 PHOSPHORUS-CONTAINING CATALYST AND METHOD FOR HYDROPROCESSING OIL LOADS WITH THIS CATALYST
PCT/FR1997/002006 WO1998020969A1 (en) 1996-11-13 1997-11-07 Catalyst containing phosphorus and method for hydro-treating oil feedstocks with this catalyst

Publications (2)

Publication Number Publication Date
AU5058598A true AU5058598A (en) 1998-06-03
AU731209B2 AU731209B2 (en) 2001-03-29

Family

ID=9497550

Family Applications (1)

Application Number Title Priority Date Filing Date
AU50585/98A Ceased AU731209B2 (en) 1996-11-13 1997-11-07 Catalyst containing phosphorous and a process for hydrotreatment of petroleum feeds using the catalyst

Country Status (14)

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

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2288035C1 (en) * 2005-12-02 2006-11-27 Открытое акционерное общество "Ангарский завод катализаторов и органического синтеза" (ОАО АЗКиОС) Presulfidized catalyst for hydrofining of petroleum fractions
RU2306978C1 (en) * 2006-03-24 2007-09-27 Открытое акционерное общество "Ангарский завод катализаторов и органического синтеза" (ОАО АКЗиОС) Petroleum fractions hydrofining catalyst and a method for preparation thereof
CN101428213B (en) * 2007-11-07 2011-04-20 中国科学院大连化学物理研究所 Uses of carbon carried noble metal catalysts in cellulose hydrogenation hydrolytic reaction
CN101428214B (en) * 2007-11-07 2011-01-19 中国科学院大连化学物理研究所 Application of Alumina Supported Noble Metal Catalysts in Cellulose Hydrohydrolysis
RU2387475C1 (en) * 2008-11-20 2010-04-27 Институт катализа им. Г.К. Борескова Сибирского отделения Российской академии наук (статус государственного учреждения) Catalyst, method of preparing said catalyst and process for hydrofining hydrocarbon material
FR2998488B1 (en) * 2012-11-29 2015-02-06 Ifp Energies Now HYDROTREATMENT CATALYST FROM ALUMIN GEL AND METHOD OF PREPARING SUCH A CATALYST
FR3022156B1 (en) * 2014-06-13 2018-02-23 Ifp Energies Now CATALYST AND MACROPOROUS CATALYST WITH COMALATED ACTIVE PHASE, PROCESS FOR THE PREPARATION THEREOF AND USE THEREOF IN HYDROTREATMENT OF RESIDUES
RU2616601C1 (en) * 2016-03-10 2017-04-18 Открытое акционерное общество "Нефтяная компания "Роснефть" Catalyst for vacuum gas oil hydrotreating, and process for preparation (versions)
RU2620267C1 (en) * 2016-03-17 2017-05-24 Открытое акционерное общество "Нефтяная компания "Роснефть" Catalyst for vacuum gas oil hydrotreating and method of preparation thereof
US12071592B2 (en) 2017-02-12 2024-08-27 Magēmā Technology LLC Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil
US12025435B2 (en) 2017-02-12 2024-07-02 Magēmã Technology LLC Multi-stage device and process for production of a low sulfur heavy marine fuel oil
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
US12281266B2 (en) 2017-02-12 2025-04-22 Magẽmã Technology LLC Heavy marine fuel oil composition
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
RU2712446C1 (en) * 2019-07-30 2020-01-29 Акционерное общество "Специальное конструкторско-технологическое бюро "Катализатор" Method of preparing carrier for catalysts based on aluminum oxide

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US469675A (en) * 1892-03-01 Type-writing machine
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 (en) * 1988-04-21 1989-10-30 Sumitomo Metal Mining Co Ltd Catalyst for hydrotreating hydrocarbons
US4940530A (en) * 1989-02-21 1990-07-10 Amoco Corporation Two-stage hydrocarbon conversion process
ES2086476T3 (en) * 1990-08-03 1996-07-01 Akzo Nobel Nv HYDRODESULFURATION PROCEDURE.
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
FR2755625B1 (en) 1998-12-11
DE69724820T2 (en) 2004-04-08
CA2270590A1 (en) 1998-05-22
DE69724820D1 (en) 2003-10-16
CN1237919A (en) 1999-12-08
CN1108190C (en) 2003-05-14
NZ335179A (en) 2000-12-22
JP2001503328A (en) 2001-03-13
DK0952888T3 (en) 2004-01-05
BR9713345A (en) 2000-05-09
FR2755625A1 (en) 1998-05-15
EP0952888A1 (en) 1999-11-03
KR100473668B1 (en) 2005-03-07
ATE249276T1 (en) 2003-09-15
WO1998020969A1 (en) 1998-05-22
RU2192923C2 (en) 2002-11-20
EP0952888B1 (en) 2003-09-10
KR20000053177A (en) 2000-08-25

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Legal Events

Date Code Title Description
FGA Letters patent sealed or granted (standard patent)
MK14 Patent ceased section 143(a) (annual fees not paid) or expired