NZ335179A - Macropore catalysts containing cobalt, molybdenum and phosphorus for hydro-treating oil feedstocks - Google Patents

Macropore catalysts containing cobalt, molybdenum and phosphorus for hydro-treating oil feedstocks

Info

Publication number
NZ335179A
NZ335179A NZ335179A NZ33517997A NZ335179A NZ 335179 A NZ335179 A NZ 335179A NZ 335179 A NZ335179 A NZ 335179A NZ 33517997 A NZ33517997 A NZ 33517997A NZ 335179 A NZ335179 A NZ 335179A
Authority
NZ
New Zealand
Prior art keywords
hydro
phosphorus
molybdenum
macropore
containing cobalt
Prior art date
Application number
NZ335179A
Inventor
Samuel Mignard
Nathalie George-Marchal
Virginie Harle
Slavik Kasztelan
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
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=NZ335179(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 filed Critical Inst Francais Du Petrole
Publication of NZ335179A publication Critical patent/NZ335179A/en

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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/615100-500 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64Pore diameter
    • B01J35/6472-50 nm
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66Pore distribution
    • 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

Landscapes

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

Abstract

Provided is 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, The catalyst has a BET surface between 100-300 m2/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 is 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 specification also concerns a hydro-treating method using this catalyst, and in particular of hydrodesulphuration.
NZ335179A 1996-11-13 1997-11-07 Macropore catalysts containing cobalt, molybdenum and phosphorus for hydro-treating oil feedstocks NZ335179A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
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 (1)

Publication Number Publication Date
NZ335179A true NZ335179A (en) 2000-12-22

Family

ID=9497550

Family Applications (1)

Application Number Title Priority Date Filing Date
NZ335179A NZ335179A (en) 1996-11-13 1997-11-07 Macropore catalysts containing cobalt, molybdenum and phosphorus for hydro-treating oil feedstocks

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 (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101428214B (en) * 2007-11-07 2011-01-19 中国科学院大连化学物理研究所 Uses of aluminum oxide supported noble metal catalyst in cellulose hydrogenation hydrolyzation
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
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
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
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
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
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
US20180230389A1 (en) 2017-02-12 2018-08-16 Magēmā Technology, LLC Multi-Stage Process and Device for Reducing Environmental Contaminates in Heavy Marine Fuel Oil
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 (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 (en) * 1988-04-21 1989-10-30 Sumitomo Metal Mining Co Ltd Catalyst for hydrogenation treatment of hydrocarbon
US4940530A (en) * 1989-02-21 1990-07-10 Amoco Corporation Two-stage hydrocarbon conversion process
ATE137686T1 (en) * 1990-08-03 1996-05-15 Akzo Nobel Nv METHOD FOR HYDROGENATE DESULFURIZATION
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
DE69724820T2 (en) 2004-04-08
KR20000053177A (en) 2000-08-25
ATE249276T1 (en) 2003-09-15
DE69724820D1 (en) 2003-10-16
KR100473668B1 (en) 2005-03-07
AU731209B2 (en) 2001-03-29
CN1108190C (en) 2003-05-14
RU2192923C2 (en) 2002-11-20
JP2001503328A (en) 2001-03-13
EP0952888A1 (en) 1999-11-03
EP0952888B1 (en) 2003-09-10
AU5058598A (en) 1998-06-03
WO1998020969A1 (en) 1998-05-22
DK0952888T3 (en) 2004-01-05
CN1237919A (en) 1999-12-08
FR2755625A1 (en) 1998-05-15
FR2755625B1 (en) 1998-12-11
BR9713345A (en) 2000-05-09
CA2270590A1 (en) 1998-05-22

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