CA2508605C - Procede d'hydrotraitement de charge lourde reposant sur l'utilisation d'un melange de catalyseurs - Google Patents

Procede d'hydrotraitement de charge lourde reposant sur l'utilisation d'un melange de catalyseurs Download PDF

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Publication number
CA2508605C
CA2508605C CA2508605A CA2508605A CA2508605C CA 2508605 C CA2508605 C CA 2508605C CA 2508605 A CA2508605 A CA 2508605A CA 2508605 A CA2508605 A CA 2508605A CA 2508605 C CA2508605 C CA 2508605C
Authority
CA
Canada
Prior art keywords
catalyst
pore volume
pores
diameter
ang
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.)
Expired - Lifetime
Application number
CA2508605A
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English (en)
Other versions
CA2508605A1 (fr
Inventor
Frans Lodewijk Plantenga
Katsuhisa Fujita
Satoshi Abe
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.)
Nippon Ketjen Co Ltd
Albemarle Netherlands BV
Original Assignee
Nippon Ketjen Co Ltd
Albemarle Netherlands BV
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 Nippon Ketjen Co Ltd, Albemarle Netherlands BV filed Critical Nippon Ketjen Co Ltd
Publication of CA2508605A1 publication Critical patent/CA2508605A1/fr
Application granted granted Critical
Publication of CA2508605C publication Critical patent/CA2508605C/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

Landscapes

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

Abstract

L'invention concerne un procédé d'hydrotraitement de charges d'hydrocarbures lourds, de préférence en réacteur à combustible en suspension, par contact entre la charge et un mélange de deux catalyseurs d'hydrotraitement qui satisfont des conditions spécifiées relatives à la distribution de la taille des pores. Plus précisément, le catalyseur I comporte au moins 50 % du volume total de pores en pores ayant un diamètre d'au moins 20 nm (200 .ANG.), et de 10 à 30 % du volume total de pores en pores ayant un diamètre d'au moins 200 nm (2000 .ANG.), tandis que le catalyseur II comporte au moins 75 % du volume total de pores en pores ayant un diamètre compris entre 10 et 120 nm (100-1200 .ANG.), de 0 à 2 % du volume total de pores en pores ayant un diamètre d'au moins 400 nm (4000 .ANG.), et de 0 à 1 % du volume total de pores en pores ayant un diamètre d'au moins 1000 nm (10000 .ANG.). Le procédé décrit combine un degré élevé d'élimination des contaminants, un degré de conversion élevé, un faible degré de formation de sédiments, et un degré élevé de flexibilité de traitement.
CA2508605A 2002-12-06 2003-12-04 Procede d'hydrotraitement de charge lourde reposant sur l'utilisation d'un melange de catalyseurs Expired - Lifetime CA2508605C (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP02080141 2002-12-06
EP02080141.1 2002-12-06
PCT/EP2003/013791 WO2004052534A1 (fr) 2002-12-06 2003-12-04 Procede d'hydrotraitement de charge lourde reposant sur l'utilisation d'un melange de catalyseurs

Publications (2)

Publication Number Publication Date
CA2508605A1 CA2508605A1 (fr) 2004-06-24
CA2508605C true CA2508605C (fr) 2011-11-29

Family

ID=32479753

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2508605A Expired - Lifetime CA2508605C (fr) 2002-12-06 2003-12-04 Procede d'hydrotraitement de charge lourde reposant sur l'utilisation d'un melange de catalyseurs

Country Status (8)

Country Link
EP (1) EP1567262B1 (fr)
JP (1) JP4369871B2 (fr)
CN (1) CN100444956C (fr)
AU (1) AU2003289969A1 (fr)
CA (1) CA2508605C (fr)
ES (1) ES2859557T3 (fr)
PL (1) PL213492B1 (fr)
WO (1) WO2004052534A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11090638B2 (en) 2011-12-22 2021-08-17 Advanced Refining Technologies Llc Silica containing alumina supports, catalysts made therefrom and processes using the same

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JP4822705B2 (ja) * 2004-12-24 2011-11-24 日揮触媒化成株式会社 重質炭化水素油の水素化処理触媒組成物およびその製造方法
CN101942317B (zh) * 2009-07-09 2013-08-28 中国石油化工股份有限公司 一种沸腾床催化剂的级配方法
CN102465010B (zh) * 2010-11-04 2014-05-21 中国石油化工股份有限公司 一种重质、劣质原料加氢处理方法
CN102443414B (zh) * 2010-10-13 2014-05-21 中国石油化工股份有限公司 重质原料油沸腾床加氢处理方法
CN104560138B (zh) * 2013-10-22 2016-10-26 中国石油化工股份有限公司 一种沸腾床重油加氢处理方法
US10507459B2 (en) * 2013-11-25 2019-12-17 Shell Oil Company Process for the catalytic conversion of micro carbon residue content of heavy hydrocarbon feedstocks and a low surface area catalyst composition for use therein
FR3022236B1 (fr) 2014-06-13 2016-07-08 Ifp Energies Now Alumine mesoporeuse et macroporeuse amorphe a distribution poreuse optimisee et son procede de preparation
FR3022157B1 (fr) 2014-06-13 2017-09-01 Ifp Energies Now Catalyseur bimodal a phase active comalaxee, son procede de preparation et son utilisation en hydrotraitement de residus
FR3022159B1 (fr) 2014-06-13 2018-04-27 IFP Energies Nouvelles Catalyseur mesoporeux et macroporeux d'hydroconversion de residus et methode de preparation
FR3037054B1 (fr) 2015-06-05 2021-08-27 Ifp Energies Now Procede de preparation d'une boehmite presentant des cristallites particulieres
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
US12559689B2 (en) 2017-02-12 2026-02-24 Magēmā Technology LLC Multi-stage process and device for treatment heavy marine fuel and resultant composition and the removal of detrimental solids
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
US12281266B2 (en) 2017-02-12 2025-04-22 Magẽmã Technology LLC Heavy marine fuel oil composition
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
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
EP4065269A1 (fr) * 2019-11-29 2022-10-05 Rhodia Operations Alumine présentant un profil poreux particulier
CA3158808A1 (fr) * 2019-11-29 2021-06-03 Rhodia Operations Alumine presentant un profil poreux particulier

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2528721B1 (fr) * 1982-06-17 1986-02-28 Pro Catalyse Ste Fse Prod Cata Catalyseur supporte presentant une resistance accrue aux poisons et son utilisation en particulier pour l'hydrotraitement de fractions petrolieres contenant des metaux
US4534852A (en) * 1984-11-30 1985-08-13 Shell Oil Company Single-stage hydrotreating process for converting pitch to conversion process feedstock
US5100855A (en) * 1990-03-30 1992-03-31 Amoco Corporation Mixed catalyst system for hyproconversion system
CN1030328C (zh) * 1991-09-05 1995-11-22 中国石油化工总公司石油化工科学研究院 加氢催化剂的制备方法
US6086749A (en) * 1996-12-23 2000-07-11 Chevron U.S.A. Inc. Catalyst and method for hydroprocessing a hydrocarbon feed stream in a reactor containing two or more catalysts
JP4612229B2 (ja) * 2001-06-08 2011-01-12 日本ケッチェン株式会社 重質炭化水素油の水素化処理用触媒並びに水素化処理方法

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11090638B2 (en) 2011-12-22 2021-08-17 Advanced Refining Technologies Llc Silica containing alumina supports, catalysts made therefrom and processes using the same
US11642664B2 (en) 2011-12-22 2023-05-09 Advanced Refining Technologies Llc Silica containing alumina supports, catalysts made therefrom and processes using the same

Also Published As

Publication number Publication date
EP1567262B1 (fr) 2021-02-03
JP2006509084A (ja) 2006-03-16
CA2508605A1 (fr) 2004-06-24
AU2003289969A8 (en) 2004-06-30
AU2003289969A1 (en) 2004-06-30
EP1567262A1 (fr) 2005-08-31
PL213492B1 (pl) 2013-03-29
ES2859557T3 (es) 2021-10-04
WO2004052534A1 (fr) 2004-06-24
CN100444956C (zh) 2008-12-24
PL377092A1 (pl) 2006-01-23
JP4369871B2 (ja) 2009-11-25
CN1735456A (zh) 2006-02-15

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Effective date: 20231204