ATE425809T1 - Hydroraffinierungs-katalysator und hydroraffinierungs-verfahren - Google Patents

Hydroraffinierungs-katalysator und hydroraffinierungs-verfahren

Info

Publication number
ATE425809T1
ATE425809T1 AT01938551T AT01938551T ATE425809T1 AT E425809 T1 ATE425809 T1 AT E425809T1 AT 01938551 T AT01938551 T AT 01938551T AT 01938551 T AT01938551 T AT 01938551T AT E425809 T1 ATE425809 T1 AT E425809T1
Authority
AT
Austria
Prior art keywords
catalyst
hydroraffining
hydrorefining
demetalization
pore diameter
Prior art date
Application number
AT01938551T
Other languages
English (en)
Inventor
Hideaki Kumagai
Hiroki Koyama
Kenji Nakamura
Naoharu Igarashi
Takayuki Tsukada
Masayuki Mori
Original Assignee
Japan Energy Corp
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 Japan Energy Corp filed Critical Japan Energy Corp
Application granted granted Critical
Publication of ATE425809T1 publication Critical patent/ATE425809T1/de

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
    • 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
    • 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
    • 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
    • B01J27/19—Molybdenum
    • 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
    • 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
    • B01J35/64—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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (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)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
AT01938551T 2000-06-08 2001-06-07 Hydroraffinierungs-katalysator und hydroraffinierungs-verfahren ATE425809T1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000171428A JP2003171671A (ja) 2000-06-08 2000-06-08 重質油の水素化精製方法

Publications (1)

Publication Number Publication Date
ATE425809T1 true ATE425809T1 (de) 2009-04-15

Family

ID=18673979

Family Applications (2)

Application Number Title Priority Date Filing Date
AT07022873T ATE459417T1 (de) 2000-06-08 2001-06-07 Hydroraffinationsgerät für schweröl und hydroraffinationsverfahren für schweröl
AT01938551T ATE425809T1 (de) 2000-06-08 2001-06-07 Hydroraffinierungs-katalysator und hydroraffinierungs-verfahren

Family Applications Before (1)

Application Number Title Priority Date Filing Date
AT07022873T ATE459417T1 (de) 2000-06-08 2001-06-07 Hydroraffinationsgerät für schweröl und hydroraffinationsverfahren für schweröl

Country Status (9)

Country Link
US (1) US6858132B2 (de)
EP (2) EP1894625B1 (de)
JP (1) JP2003171671A (de)
KR (1) KR100781642B1 (de)
AT (2) ATE459417T1 (de)
CA (1) CA2391793C (de)
DE (2) DE60138018D1 (de)
DK (1) DK1291082T3 (de)
WO (1) WO2001094012A1 (de)

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WO2003006156A1 (en) * 2001-07-10 2003-01-23 Japan Energy Corporation Hydro-refining catalyst, carrier for use therein and method for production thereof
AU2003207232A1 (en) * 2002-02-06 2003-09-02 Japan Energy Corporation Method for preparing hydrogenation purification catalyst
BRPI0405738B1 (pt) * 2003-12-19 2014-09-23 Shell Int Research Método de produzir um produto de petróleo bruto
US20050133405A1 (en) 2003-12-19 2005-06-23 Wellington Scott L. Systems and methods of producing a crude product
US7736490B2 (en) 2003-12-19 2010-06-15 Shell Oil Company Systems, methods, and catalysts for producing a crude product
US7745369B2 (en) 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
US7744827B2 (en) * 2004-02-13 2010-06-29 United Technologies Corporation Catalytic treatment of fuel to impart coking resistance
CN101166811A (zh) 2005-04-11 2008-04-23 国际壳牌研究有限公司 生产具有降低氮含量的原油产品的方法和催化剂
CA2604012C (en) 2005-04-11 2013-11-19 Shell Internationale Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced mcr content
US7749374B2 (en) 2006-10-06 2010-07-06 Shell Oil Company Methods for producing a crude product
WO2009117800A1 (en) * 2008-03-25 2009-10-01 Uladzimir Ramanenkau Porous composite metal-ceramic materials
WO2012021259A1 (en) 2010-08-09 2012-02-16 W. R. Grace & Co.-Conn. Attrition resistant supports for fischer-tropsch catalysts and process for making the same
CN103773460B (zh) * 2012-10-24 2015-07-22 中国石油化工股份有限公司 一种页岩油柴油馏分一段串联加氢精制方法
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
FR2999454B1 (fr) * 2012-12-18 2015-02-06 IFP Energies Nouvelles Catalyseur d'hydrotraitement de residus a teneur controlee en silicium et son utilisation dans un procede d'hydroconversion de residus
FR2999453B1 (fr) * 2012-12-18 2015-02-06 IFP Energies Nouvelles Catalyseur d'hydrotraitement de residus comprenant du vanadium et son utilisation dans un procede d'hydroconversion de residus
RU2521385C1 (ru) * 2013-01-23 2014-06-27 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования Северо-Кавказский горно-металлургический институт (государственный технологически университет) (СКГМИ (ГТУ) Устройство для нейтрализации газов
TWI666310B (zh) * 2013-03-15 2019-07-21 Advanced Refining Technologies Llc 觸媒組成物、加氫處理重烴類部分之方法及製備沉澱氧化鋁組成物的方法
US10563138B2 (en) 2016-12-21 2020-02-18 Saudi Arabian Oil Company Method for optimizing catalyst loading for hydrocracking process
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 Magēmā Technology, LLC Multi-Stage Process and Device for Reducing Environmental Contaminates in Heavy Marine Fuel Oil
US20190126227A1 (en) 2017-10-30 2019-05-02 Saudi Arabian Oil Company Catalyst loading method to disperse heat in hydroconversion reactor
JP7321790B2 (ja) * 2019-06-25 2023-08-07 日揮触媒化成株式会社 重質油の水素化処理方法

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US4306964A (en) * 1980-09-16 1981-12-22 Mobil Oil Corporation Multi-stage process for demetalation and desulfurization of petroleum oils
US4434048A (en) * 1980-11-21 1984-02-28 The Lummus Company Hydrotreating catalyst and use thereof
JPS614533A (ja) 1984-06-15 1986-01-10 Res Assoc Residual Oil Process<Rarop> 水素化処理触媒およびこれを用いた重質鉱油の水素化脱硫分解方法
US4743572A (en) 1986-12-05 1988-05-10 Mobil Oil Corporation Magnesia-alumina-aluminum phosphate catalyst and catalyst product thereof
US4941964A (en) * 1988-03-14 1990-07-17 Texaco Inc. Hydrotreatment process employing catalyst with specified pore size distribution
JPH0295443A (ja) 1988-09-30 1990-04-06 Nippon Oil Co Ltd 残油の水素化処理触媒
US5192734A (en) * 1991-10-25 1993-03-09 W. R. Grace & Co.- Conn. Hydroprocessing catalyst composition
US5399259A (en) * 1992-04-20 1995-03-21 Texaco Inc. Hydroconversion process employing catalyst with specified pore size distribution
JPH0753968A (ja) 1993-08-09 1995-02-28 Idemitsu Kosan Co Ltd 重質炭化水素油の水素化処理方法
JP2958234B2 (ja) 1994-02-19 1999-10-06 株式会社コスモ総合研究所 重質炭化水素油の水素化処理方法
JP3462560B2 (ja) * 1994-03-04 2003-11-05 日本パイオニクス株式会社 水素ガスの精製方法
US5620592A (en) * 1994-07-29 1997-04-15 Chevron U.S.A. Inc. Low macropore resid conversion catalyst
JPH1086653A (ja) * 1996-09-17 1998-04-07 Calsonic Corp クーリングユニット
ATE296679T1 (de) 1998-12-08 2005-06-15 Japan Energy Corp Katalysator zur hydrodesulforierung und verfahren zu seiner herstellung
US6589908B1 (en) * 2000-11-28 2003-07-08 Shell Oil Company Method of making alumina having bimodal pore structure, and catalysts made therefrom

Also Published As

Publication number Publication date
EP1894625A3 (de) 2008-10-01
EP1894625B1 (de) 2010-03-03
US6858132B2 (en) 2005-02-22
DE60141488D1 (de) 2010-04-15
EP1291082A4 (de) 2004-06-30
DE60138018D1 (de) 2009-04-30
KR100781642B1 (ko) 2007-12-03
CA2391793C (en) 2011-04-05
US20020155045A1 (en) 2002-10-24
WO2001094012A1 (fr) 2001-12-13
JP2003171671A (ja) 2003-06-20
EP1894625A2 (de) 2008-03-05
DK1291082T3 (da) 2009-05-25
CA2391793A1 (en) 2001-12-13
KR20020051917A (ko) 2002-06-29
EP1291082B1 (de) 2009-03-18
EP1291082A1 (de) 2003-03-12
ATE459417T1 (de) 2010-03-15

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