ES2099804T3 - Procedimiento y dispositivo de intercambio termico de particulas solidas para regeneracion en craqueo catalitico. - Google Patents

Procedimiento y dispositivo de intercambio termico de particulas solidas para regeneracion en craqueo catalitico.

Info

Publication number
ES2099804T3
ES2099804T3 ES92401105T ES92401105T ES2099804T3 ES 2099804 T3 ES2099804 T3 ES 2099804T3 ES 92401105 T ES92401105 T ES 92401105T ES 92401105 T ES92401105 T ES 92401105T ES 2099804 T3 ES2099804 T3 ES 2099804T3
Authority
ES
Spain
Prior art keywords
regenerator
regeneration
dense
gases
bed
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
ES92401105T
Other languages
English (en)
Inventor
Frederic Hoffmann
Regis Bonifay
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
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Application granted granted Critical
Publication of ES2099804T3 publication Critical patent/ES2099804T3/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
    • 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
    • B01J38/30—Treating with free oxygen-containing gas in gaseous suspension, e.g. fluidised bed
    • B01J38/32—Indirectly heating or cooling material within regeneration zone or prior to entry into regeneration zone
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • C10G11/182—Regeneration
    • 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
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling the reactor
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00141—Coils

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

LA INVENCION SE REFIERE A UN PROCESO Y A UN DISPOSITIVO DE REGENERACION EN LECHO FLUIDO DE UN CATALIZADOR QUE CONTIENE COQUE. EL CATALIZADOR Y UNA PARTE DE LOS HUMOS DE REGENERACION SON TOMADOS EN EL LECHO DENSO DE UN REGENERADOR (1) E INTRODUCIDOS POR GRAVEDAD EN UN INTERCAMBIADOR EXTERNO EN UN PUNTO DE UNION POR DEBAJO DEL NIVEL DEL LECHO DENSO DEL REGENERADOR. EL INTERCAMBIO TERMICO SE REALIZA EN LA PARTE INFERIOR DEL INTERCAMBIADOR POR DEBAJO DEL PUNTO DE UNION. SE REALIZA DESDE EL EXTREMO INFERIOR DEL INTERCAMBIADOR HASTA POR ENCIMA DEL PUNTO DE UNION UNA ZONA DE LECHO DENSO CUYO NIVEL SE ESTABLECE SENSIBLEMENTE A LA ALTURA DEL LECHO DENSO EN EL REGENERADOR Y UNA ZONA DE DESENGANCHE (15) DE LOS GASES DE REGENERACION Y DEL GAS DE FLUIDIZACION, DE VOLUMEN APROPIADO. LOS GASES Y HUMOS SON EVACUADOS EN LA FASE (18) FLUIDIZADA DILUIDA DEL REGENERADOR POR UN CONDUCTO (17) MIENTRAS QUE EL CATALIZADOR ES RECICLADO EN EL LECHO DENSO DEL REGENERADOR POR UN CONDUCTO (25) DISTINTO DONDE CIRCULA AIRE DE FLUIDIZACION. APLICACION EN LA REGENERACION DE CATALIZADORES DE CRAQUEO EN LECHO FLUIDO
ES92401105T 1991-04-26 1992-04-17 Procedimiento y dispositivo de intercambio termico de particulas solidas para regeneracion en craqueo catalitico. Expired - Lifetime ES2099804T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9105282A FR2675714B1 (fr) 1991-04-26 1991-04-26 Procede et dispositif d'echange thermique de particules solides pour regeneration en craquage catalytique.

Publications (1)

Publication Number Publication Date
ES2099804T3 true ES2099804T3 (es) 1997-06-01

Family

ID=9412376

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92401105T Expired - Lifetime ES2099804T3 (es) 1991-04-26 1992-04-17 Procedimiento y dispositivo de intercambio termico de particulas solidas para regeneracion en craqueo catalitico.

Country Status (8)

Country Link
US (1) US5286690A (es)
EP (1) EP0511071B1 (es)
JP (1) JP3366998B2 (es)
KR (1) KR100214768B1 (es)
DE (1) DE69217111T2 (es)
ES (1) ES2099804T3 (es)
FR (1) FR2675714B1 (es)
RU (1) RU2054964C1 (es)

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2683743B1 (fr) * 1991-11-14 1994-02-11 Institut Francais Petrole Procede et dispositif d'echange thermique de particules solides pour double regeneration en craquage catalytique.
FR2705142B1 (fr) * 1993-05-10 1995-10-27 Inst Francais Du Petrole Procede de regulation du niveau thermique d'un solide dans un echangeur de chaleur presentant des nappes cylindriques de tubes.
US5800697A (en) * 1995-06-19 1998-09-01 Uop Llc FCC process with dual function catalyst cooling
FR2791354B1 (fr) 1999-03-25 2003-06-13 Inst Francais Du Petrole Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydroconversion en lits bouillonnants et une etape d'hydrotraitement
EP1043384A3 (en) * 1999-04-09 2001-05-30 Bar-Co Processes Joint Venture Improved residual oil fluid catalytic cracking process with catalyst having increased metals tolerance
EP1299505B1 (en) * 2000-07-12 2003-11-26 Shell Internationale Researchmaatschappij B.V. Standpipe inlet for enhancing particulate solids circulation for petrochemical and other processes
RU2262527C1 (ru) * 2004-05-18 2005-10-20 Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез" Способ каталитического крекинга тяжелых нефтяных фракций
US20060231461A1 (en) * 2004-08-10 2006-10-19 Weijian Mo Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock
RU2394065C2 (ru) * 2004-11-02 2010-07-10 В.Р.Грейс Энд Ко.-Конн. СПОСОБ СОКРАЩЕНИЯ ВЫБРОСОВ NOx В ПРОЦЕССАХ ПОЛНОГО СЖИГАНИЯ ПРОДУКТОВ КРЕКИНГА
US7758820B2 (en) * 2006-12-21 2010-07-20 Uop Llc Apparatus and process for regenerator mixing
RU2463335C2 (ru) * 2007-04-30 2012-10-10 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Установка и способ получения средних дистиллятов и низших олефинов из углеводородного сырья
US20100324232A1 (en) * 2007-10-10 2010-12-23 Weijian Mo Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
RU2010121906A (ru) * 2007-10-31 2013-01-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Установки и способы для получения среднедистиллятного продукта и низших олефинов из углеводородного исходного сырья
US20110034647A1 (en) * 2007-11-29 2011-02-10 Weijian Mo Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
EP2649158A2 (en) * 2010-12-10 2013-10-16 Shell Oil Company Process for treating a hydrocarbon-containing feed
US8858784B2 (en) 2010-12-10 2014-10-14 Shell Oil Company Process for treating a hydrocarbon-containing feed
FR2969651B1 (fr) 2010-12-24 2014-02-21 Total Raffinage Marketing Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par decontamination, hydroconversion en lit bouillonnant, et fractionnement par distillation atmospherique
FR2969650B1 (fr) 2010-12-24 2014-04-11 Total Raffinage Marketing Procede de conversion de charge hydrocarbonee comprenant une huile de schiste par hydroconversion en lit bouillonnant, fractionnement par distillation atmospherique et extraction liquide/liquide de la fraction lourde
WO2012118710A2 (en) * 2011-02-28 2012-09-07 Uop Llc Process and apparatus for venting a catalyst cooler
CN102827635B (zh) * 2011-06-15 2014-04-02 石宝珍 一种催化裂化方法及装置
FR2981659B1 (fr) 2011-10-20 2013-11-01 Ifp Energies Now Procede de conversion de charges petrolieres comprenant une etape d'hydroconversion en lit bouillonnant et une etape d'hydrotraitement en lit fixe pour la production de fiouls a basse teneur en soufre
FR2983866B1 (fr) 2011-12-07 2015-01-16 Ifp Energies Now Procede d'hydroconversion de charges petrolieres en lits fixes pour la production de fiouls a basse teneur en soufre
FR2999600B1 (fr) 2012-12-18 2015-11-13 IFP Energies Nouvelles Procede de raffinage d'une charge hydrocarbonee lourde mettant en oeuvre un desasphaltage selectif
FR3000098B1 (fr) 2012-12-20 2014-12-26 IFP Energies Nouvelles Procede avec separation de traitement de charges petrolieres pour la production de fiouls a basse teneur en soufre
FR3000097B1 (fr) 2012-12-20 2014-12-26 Ifp Energies Now Procede integre de traitement de charges petrolieres pour la production de fiouls a basse teneur en soufre
US10563932B2 (en) 2017-12-21 2020-02-18 Uop Llc Process and apparatus for cooling catalyst

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2735802A (en) * 1956-02-21 jahnig
US4434245A (en) * 1981-06-15 1984-02-28 Uop Inc. Fluid particle cooling process and apparatus
US4615992A (en) * 1985-04-02 1986-10-07 Air Products And Chemicals, Inc. Catalyst regeneration process with improved catalyst distribution in a fluidized bed
US4614726A (en) * 1985-06-21 1986-09-30 Ashland Oil, Inc. Process for cooling during regeneration of fluid cracking catalyst
US4923834A (en) * 1989-03-17 1990-05-08 Uop Side mounted coolers with improved backmix cooling in FCC regeneration

Also Published As

Publication number Publication date
DE69217111T2 (de) 1997-06-26
EP0511071A1 (fr) 1992-10-28
EP0511071B1 (fr) 1997-01-29
US5286690A (en) 1994-02-15
DE69217111D1 (de) 1997-03-13
RU2054964C1 (ru) 1996-02-27
JP3366998B2 (ja) 2003-01-14
JPH05123587A (ja) 1993-05-21
KR100214768B1 (ko) 1999-08-02
KR920019418A (ko) 1992-11-19
FR2675714A1 (fr) 1992-10-30
FR2675714B1 (fr) 1993-07-16

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