ES2180126T3 - Procedimiento y recinto para la regeneracion de un catalizador que incluye un control del final de la combustion. - Google Patents

Procedimiento y recinto para la regeneracion de un catalizador que incluye un control del final de la combustion.

Info

Publication number
ES2180126T3
ES2180126T3 ES98400845T ES98400845T ES2180126T3 ES 2180126 T3 ES2180126 T3 ES 2180126T3 ES 98400845 T ES98400845 T ES 98400845T ES 98400845 T ES98400845 T ES 98400845T ES 2180126 T3 ES2180126 T3 ES 2180126T3
Authority
ES
Spain
Prior art keywords
catalyst
regeneration
end control
enclosure
procedure
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
ES98400845T
Other languages
English (en)
Inventor
Francois-Xavier Brunet
Emmanuelle Bromet
Jean-Marie Deves
Dominique Humeau
Eric Sanchez
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
Priority claimed from FR9704661A external-priority patent/FR2761908B1/fr
Priority claimed from FR9704659A external-priority patent/FR2761906B1/fr
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Application granted granted Critical
Publication of ES2180126T3 publication Critical patent/ES2180126T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
    • 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
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • B01J38/14—Treating with free oxygen-containing gas with control of oxygen content in oxidation gas
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006—Controlling or regulating processes
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • 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
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/02—Heat treatment
    • 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
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • 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
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • B01J38/20—Plural distinct oxidation stages
    • 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
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • B01J38/22—Moving bed, e.g. vertically or horizontally moving bulk
    • B01J38/24—Moving bed, e.g. vertically or horizontally moving bulk having mainly transverse, i.e. lateral, flow of oxygen-containing gas and material
    • 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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C10G35/10—Catalytic reforming with moving catalysts
    • C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Catalysts (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

LA INVENCION SE REFIERE A UN METODO DE REGENERACION DE UN CATALIZADOR EN LECHO FIJO O MOVIL COMO, POR EJEMPLO, UN CATALIZADOR DE REFORMING O DE PRODUCCION DE AROMATICOS; COMPRENDE UNA ETAPA DE CONTROL DEL FINAL DE LA COMBUSTION QUE SE REALIZA DESPUES DE QUE EL CATALIZADOR HAYA PASADO POR TODAS LAS ETAPAS DE COMBUSTION DEL METODO. LA ETAPA DE CONTROL SE EFECTUA INYECTANDO UN GAS QUE CONTIENE OXIGENO EN LA ZONA EN LA QUE TIENE LUGAR EL CONTROL; ESTA ETAPA SE DESARROLLA EN CONDICIONES MAS RIGUROSAS QUE LAS ETAPAS DE COMBUSTION. LA ETAPA DE CONTROL EVOLUCIONA CON UN CONSUMO DE OXIGENO INFERIOR AL 10 %. A SER POSIBLE, LA TEMPERATURA SE MANTIENE ESENCIALMENTE CONSTANTE. TAMBIEN SE REIVINDICA EL RECINTO EN EL CUAL SE DESARROLLA LA INVENCION.
ES98400845T 1997-04-14 1998-04-07 Procedimiento y recinto para la regeneracion de un catalizador que incluye un control del final de la combustion. Expired - Lifetime ES2180126T3 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9704661A FR2761908B1 (fr) 1997-04-14 1997-04-14 Procede et dispositif pour le controle de la combustion d'un catalyseur en regeneration par reperage de la position du front de flamme
FR9704659A FR2761906B1 (fr) 1997-04-14 1997-04-14 Procede et dispositif pour la regeneration d'un catalyseur incluant un controle de la fin de la combustion

Publications (1)

Publication Number Publication Date
ES2180126T3 true ES2180126T3 (es) 2003-02-01

Family

ID=26233467

Family Applications (1)

Application Number Title Priority Date Filing Date
ES98400845T Expired - Lifetime ES2180126T3 (es) 1997-04-14 1998-04-07 Procedimiento y recinto para la regeneracion de un catalizador que incluye un control del final de la combustion.

Country Status (8)

Country Link
US (3) US6239055B1 (es)
EP (1) EP0873784B1 (es)
JP (1) JP4045367B2 (es)
KR (1) KR100519211B1 (es)
CN (1) CN1117633C (es)
CA (1) CA2232613C (es)
DE (1) DE69806435T2 (es)
ES (1) ES2180126T3 (es)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2837113B1 (fr) * 2002-03-15 2004-06-18 Inst Francais Du Petrole Procede de controle d'une zone de combustion a lit mobile et son utilisation
US7291311B2 (en) * 2002-03-15 2007-11-06 Institut Francais Du Petrole Process for controlling a moving bed combustion zone and its use
WO2004043591A1 (en) * 2002-11-07 2004-05-27 Tufts University Catalyst having metal in reduced quantity and reduced cluster size
FR2877590B1 (fr) * 2004-11-09 2007-01-12 Inst Francais Du Petrole Dispositif reactionnel a plusieurs zones en lit mobile avec appoint dans chaque zone de catalyseur regenere ou frais
FR2877589B1 (fr) * 2004-11-09 2007-01-12 Inst Francais Du Petrole Reacteur a plusieurs zones en lit fixe ou mobile avec echangeur thermique integre
DE102004059647B4 (de) * 2004-12-10 2008-01-31 Webasto Ag Verfahren zum Regenerieren eines Reformers
US7585803B1 (en) * 2005-10-19 2009-09-08 Uop Llc Catalyst regeneration method
US7811447B2 (en) * 2007-08-01 2010-10-12 Uop Llc Method of transferring particles from one pressure zone to another pressure zone
CN101376099B (zh) * 2007-08-29 2010-12-15 上海华明高技术（集团）有限公司 过氧化氢工作液再生过程用的活性氧化铝再生处理方法
CN101376100B (zh) * 2007-08-29 2010-05-26 上海华明高技术（集团）有限公司 过氧化氢工作液再生过程用的活性氧化铝再生处理方法
FR2922785B1 (fr) * 2007-10-26 2009-12-11 Inst Francais Du Petrole Procede de regeneration d'un catalyseur de reformage
FR2922786B1 (fr) * 2007-10-26 2010-02-26 Inst Francais Du Petrole Procede et enceinte de regeneration d'un catalyseur de reformage
FR2934963B1 (fr) * 2008-08-13 2010-11-26 Inst Francais Du Petrole Appareil de regeneration de catalyseur et procede de regeneration associe
US8984886B2 (en) 2010-02-12 2015-03-24 General Electric Company Systems and methods of operating a catalytic reforming assembly for use with a gas turbine engine system
FR2957821B1 (fr) * 2010-03-24 2014-08-29 Inst Francais Du Petrole Nouvelle zone de regeneration du catalyseur divisee en secteurs pour unites catalytiques regeneratives
KR102124338B1 (ko) * 2019-03-11 2020-06-19 효성화학 주식회사 촉매 재생 장치 및 방법

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2344770A (en) * 1941-12-15 1944-03-21 Standard Oil Co Catalyst regeneration control
US2391327A (en) * 1942-07-22 1945-12-18 Universal Oil Prod Co Regeneration of solid contact material
US2487717A (en) * 1944-05-22 1949-11-08 California Research Corp Apparatus for controlling catalyst regeneration
US3652231A (en) * 1969-09-25 1972-03-28 Universal Oil Prod Co Reconditioning system for moving column of reforming catalyst
US4007131A (en) * 1974-01-31 1977-02-08 Mobil Oil Corporation Hydroprocessing catalyst regeneration
FR2395069A1 (fr) * 1977-06-20 1979-01-19 Inst Francais Du Petrole Procede de recyclage des reactifs gazeux utilises pour la regeneration d'un catalyseur d'hydroconversion d'hydrocarbures
US4578370A (en) * 1985-04-25 1986-03-25 Uop Inc. Gas circulation method for moving bed catalyst regeneration zones
FR2603044B1 (fr) * 1986-08-25 1988-11-04 Inst Francais Du Petrole Procede de regeneration d'un catalyseur d'hydroconversion d'hydrocarbures
US4977119A (en) * 1987-11-04 1990-12-11 Uop Method of regenerating hydrocarbon conversion catalyst by coke burning
US4872970A (en) * 1988-09-23 1989-10-10 Exxon Research And Engineering Company Reactivation of iridium-containing catalysts
DE69018487T2 (de) * 1989-01-13 1995-09-07 Inst Francais Du Petrole Verfahren zur Regenerierung eines Katalysators zur Reformierung oder zur Herstellung von aromatischen Kohlenwasserstoffen.
FR2642330B1 (fr) * 1989-02-01 1991-05-24 Inst Francais Du Petrole Procede de regeneration d'un catalyseur de reformage ou de production d'hydrocarbures aromatiques
US5053371A (en) * 1990-11-02 1991-10-01 Uop Catalyst regeneration method with three-zone combustion gas addition
US6689331B1 (en) * 1997-04-14 2004-02-10 Institut Francais du Pétrole Staged combustion process and apparatus for regenerating a reforming or aromatic compound production catalyst in a moving bed

Also Published As

Publication number Publication date
DE69806435D1 (de) 2002-08-14
EP0873784B1 (fr) 2002-07-10
JPH10286470A (ja) 1998-10-27
KR100519211B1 (ko) 2005-12-16
CA2232613C (fr) 2007-06-26
US6239055B1 (en) 2001-05-29
US6506702B2 (en) 2003-01-14
DE69806435T2 (de) 2002-11-07
KR19980081374A (ko) 1998-11-25
CN1117633C (zh) 2003-08-13
CA2232613A1 (fr) 1998-10-14
JP4045367B2 (ja) 2008-02-13
US8728404B1 (en) 2014-05-20
EP0873784A1 (fr) 1998-10-28
CN1201718A (zh) 1998-12-16
US20010049329A1 (en) 2001-12-06

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