ES2050516T3 - Procedimiento y dispositivo de craqueo catalitico en lecho fluido en corriente descendente. - Google Patents

Procedimiento y dispositivo de craqueo catalitico en lecho fluido en corriente descendente.

Info

Publication number
ES2050516T3
ES2050516T3 ES91402553T ES91402553T ES2050516T3 ES 2050516 T3 ES2050516 T3 ES 2050516T3 ES 91402553 T ES91402553 T ES 91402553T ES 91402553 T ES91402553 T ES 91402553T ES 2050516 T3 ES2050516 T3 ES 2050516T3
Authority
ES
Spain
Prior art keywords
fluid bed
procedure
catalytic cracking
down current
reactor
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
ES91402553T
Other languages
English (en)
Inventor
Renaud Pontier
Frederic Hoffmann
Pierre Galtier
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 ES2050516T3 publication Critical patent/ES2050516T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • 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
    • B01J8/1809—Controlling processes
    • 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
    • C10G11/187—Controlling or regulating

Landscapes

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

Abstract

DE CRAQUEO EN LECHO FLUIDO DE CORRIENTE DESCENDENTE. RA MAS PRECISA, SE TOMA EL CATALIZADOR AL MENOS EN PARTE REGENERADO, QUE DEBE SER RECICLADO HACIA EL REACTOR (1), A PARTIR DE UNA FASE DENSA (17A), CONTENIDA EN UN REGENERADOR (17), Y SE EFECTUA LA ETAPA DE INTRODUCCION DEL CATALIZADOR EN LA PARTE SUPERIOR (3) DEL REACTOR (1) EN CONDICIONES TALES COMO LA MASA VOLUMINICA DE LA SUSPENSION GAS-SOLIDO ASI CREADA ESTA COMPRENDIDA ENTRE 80 Y 500 KG/M ELEVADO 3 ANTES DE SU PUESTA EN CONTACTO CON LA CARGA QUE SE INTRODUCE POR LOS INYECTORES (5). LICACION EN EL CRAQUEO CATALITICO DE CARGAS PESADAS HIDROCARBONADAS.
ES91402553T 1990-10-03 1991-09-25 Procedimiento y dispositivo de craqueo catalitico en lecho fluido en corriente descendente. Expired - Lifetime ES2050516T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9012275A FR2667609B1 (fr) 1990-10-03 1990-10-03 Procede et dispositif de craquage catalytique en lit fluide a courant descendant.

Publications (1)

Publication Number Publication Date
ES2050516T3 true ES2050516T3 (es) 1994-05-16

Family

ID=9400957

Family Applications (1)

Application Number Title Priority Date Filing Date
ES91402553T Expired - Lifetime ES2050516T3 (es) 1990-10-03 1991-09-25 Procedimiento y dispositivo de craqueo catalitico en lecho fluido en corriente descendente.

Country Status (9)

Country Link
US (2) US5344554A (es)
EP (1) EP0479645B1 (es)
JP (1) JP3028383B2 (es)
KR (1) KR100193312B1 (es)
CA (1) CA2052520C (es)
DE (1) DE69100996T2 (es)
ES (1) ES2050516T3 (es)
FR (1) FR2667609B1 (es)
ZA (1) ZA917877B (es)

Families Citing this family (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2715163B1 (fr) * 1994-01-18 1996-04-05 Total Raffinage Distribution Procédé de craquage catalytique en lit fluidisé d'une charge d'hydrocarbures, notamment d'une charge à forte teneur en composés azotés basiques.
US5582712A (en) * 1994-04-29 1996-12-10 Uop Downflow FCC reaction arrangement with upflow regeneration
US5549815A (en) * 1994-05-20 1996-08-27 Exxon Research And Engineering Company Method for fluidizing a dense phase bed of solids
US5843377A (en) * 1996-08-26 1998-12-01 Uop Llc Contained separation system for FCC reaction downcomer
FR2753453B1 (fr) * 1996-09-18 1998-12-04 Total Raffinage Distribution Procede et dispositif de craquage catalytique en lit fluidise d'une charge d'hydrocarbures, mettant en oeuvre une zone de mise en contact amelioree
FR2753454B1 (fr) * 1996-09-18 1999-06-04 Inst Francais Du Petrole Procede et dispositif de craquage catalytique descendant mettant en oeuvre l'injection d'une charge sous un angle adequat sur un catalyseur conditionne
JP3574555B2 (ja) * 1996-11-15 2004-10-06 新日本石油株式会社 重質油の流動接触分解方法
US6187272B1 (en) 1997-03-13 2001-02-13 Nippon Mitsubishi Oil Corporation Recycling fluidization system
JP3553311B2 (ja) * 1997-03-14 2004-08-11 財団法人石油産業活性化センター 炭化水素油の接触分解方法
US6186658B1 (en) * 1997-03-14 2001-02-13 Nippon Mitsubishi Oil Corporation Apparatus for mixing a fluid feedstock with particles
FR2785907B1 (fr) * 1998-11-13 2001-01-05 Inst Francais Du Petrole Procede et dispositif de craquage catalytique comprenant des reacteurs a ecoulements descendant et ascendant
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
FR2802211B1 (fr) * 1999-12-14 2002-02-01 Inst Francais Du Petrole Procede et dispositif de craquage catalytique comprenant en parallele au moins un reacteur a ecoulement ascendant et au moins un reacteur a ecoulement descendant
BR0101433B1 (pt) * 2001-04-10 2011-02-22 método e dispositivo de entrada multi-funcional para reator tubular de fluxo descendente.
BR0210168A (pt) * 2001-06-08 2004-04-27 Petroleo Brasileiro Sa Processo para craqueamento catalìtico fluido
KR20030010364A (ko) * 2001-07-26 2003-02-05 김동춘 촉매 하행식 크래킹반응 유화설비 및 이를 이용한휘발유·경유의 제조방법
KR100517898B1 (ko) * 2001-07-31 2005-09-30 김범진 폐합성수지를 원료로 하는 촉매 하행식 크래킹반응기 및 이를 이용한 휘발유·경유의 제조방법
US6534689B1 (en) 2001-08-24 2003-03-18 Pyrocat Ltd. Process for the conversion of waste plastics to produce hydrocarbon oils
CN1205305C (zh) * 2001-11-29 2005-06-08 中国石油化工股份有限公司 一种催化裂化反应－再生系统
CN1309804C (zh) * 2004-09-03 2007-04-11 中国石油化工集团公司 一种下行管式催化裂化方法和装置
US20060118465A1 (en) * 2004-12-02 2006-06-08 The University Of Western Ontario Catalytic sulfur removal from a hydrocarbon stream
US20080011644A1 (en) * 2006-07-13 2008-01-17 Dean Christopher F Ancillary cracking of heavy oils in conjuction with FCC unit operations
US20080011645A1 (en) * 2006-07-13 2008-01-17 Dean Christopher F Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations
US7600950B2 (en) * 2007-11-30 2009-10-13 Uop Llc Device to transfer catalyst from a low pressure vessel to a high pressure vessel and purge the transferred catalyst
US8075227B2 (en) * 2007-11-30 2011-12-13 Uop Llc Device to transfer catalyst from a low pressure vessel to a high pressure vessel and purge the transferred catalyst
MY156346A (en) * 2008-06-04 2016-02-15 Inbicon As Devices and methods for discharging pretreated biomass from higher to lower pressure regions
CN103814114B (zh) 2011-07-27 2018-04-24 沙特阿拉伯石油公司 在下流式反应器中流化催化裂化链烷烃族石脑油
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
WO2017105786A1 (en) * 2015-12-16 2017-06-22 Uop Llc Method and apparatus for catalyst sampling
US10767117B2 (en) 2017-04-25 2020-09-08 Saudi Arabian Oil Company Enhanced light olefin yield via steam catalytic downer pyrolysis of hydrocarbon feedstock
US11471848B1 (en) * 2021-10-22 2022-10-18 Advanced Fusion Systems Llc Universal chemical processor

Family Cites Families (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2781234A (en) * 1954-05-18 1957-02-12 Exxon Research Engineering Co Automatic control of standpipe and u-bend aeration
US2965454A (en) * 1957-04-30 1960-12-20 Phillips Petroleum Co Fluidized conversion and stripping apparatus
US3850582A (en) * 1969-12-10 1974-11-26 Exxon Research Engineering Co Apparatus for controlled addition of fluidized particles to a processing unit
US3835029A (en) * 1972-04-24 1974-09-10 Phillips Petroleum Co Downflow concurrent catalytic cracking
US3963603A (en) * 1973-06-08 1976-06-15 Texaco Inc. Fluid catalytic cracking
US4062759A (en) * 1976-05-07 1977-12-13 Texaco Inc. Fluidized catalytic cracking regeneration process
US4035153A (en) * 1976-05-07 1977-07-12 Texaco Inc. Fluidized cracking catalyst regeneration apparatus
US4327055A (en) * 1979-12-31 1982-04-27 Exxon Research & Engineering Co. Continuous catalyst unloading device
US4385985A (en) * 1981-04-14 1983-05-31 Mobil Oil Corporation FCC Reactor with a downflow reactor riser
US4459071A (en) * 1982-01-25 1984-07-10 Stone & Webster Engineering Corp. Solids flow regulator
US4532026A (en) * 1982-07-06 1985-07-30 Chevron Research Company Method to improve circulation control in fluidized systems
US4453865A (en) * 1982-07-21 1984-06-12 Stone & Webster Engineering Corp. Automatic pressure sensitive regulation assembly
US4793913A (en) * 1983-02-04 1988-12-27 Chevron Research Company Method for liquid feed dispersion in fluid catalytic cracking systems
US4514285A (en) * 1983-03-23 1985-04-30 Texaco Inc. Catalytic cracking system
US4824557A (en) * 1984-07-09 1989-04-25 Amoco Corporation Process for mixing cracking catalyst with a fluid hydrocarbon
US4849091A (en) * 1986-09-17 1989-07-18 Uop Partial CO combustion with staged regeneration of catalyst
US5106587A (en) * 1987-08-11 1992-04-21 Stone & Webster Engineering Corp. Particulate solids cracking apparatus
US5106799A (en) * 1988-04-12 1992-04-21 Mobil Oil Corporation Fluidized bed combustion process
US4902407A (en) * 1988-06-09 1990-02-20 Texaco Inc. Catalyst inventory control in an ebullated bed process
US5081039A (en) * 1989-11-16 1992-01-14 Amoco Corporation Process for making catalyst inventory measurements and control procedure for adding or withdrawing catalyst
FR2655053B1 (fr) * 1989-11-24 1994-04-29 Inst Francais Du Petrole Procede et dispositif de regulation des conditions de fonctionnement d'un reacteur de craquage catalytique utilisant une source de rayonnements ionisants.

Also Published As

Publication number Publication date
US5344554A (en) 1994-09-06
KR100193312B1 (ko) 1999-06-15
JPH04261494A (ja) 1992-09-17
EP0479645B1 (fr) 1994-01-12
DE69100996D1 (de) 1994-02-24
DE69100996T2 (de) 1994-05-05
CA2052520A1 (fr) 1992-04-04
JP3028383B2 (ja) 2000-04-04
KR920008169A (ko) 1992-05-27
CA2052520C (fr) 2002-05-28
ZA917877B (en) 1993-04-02
FR2667609B1 (fr) 1993-07-16
EP0479645A1 (fr) 1992-04-08
FR2667609A1 (fr) 1992-04-10
US5449496A (en) 1995-09-12

Similar Documents

Publication Publication Date Title
ES2050516T3 (es) Procedimiento y dispositivo de craqueo catalitico en lecho fluido en corriente descendente.
TW354264B (en) Temperature swing adsorption
AR248227A1 (es) Disposicion distribuidora de catalizador usado destinada para una unidad de craqueo con catalizador fluido.
CA1106699A (en) Swivel-truck spring system for railroad use
AR038135A1 (es) Regeneracion de catalizador
DE3462089D1 (en) Process for drying gas streams
ES2044096T3 (es) Tratamiento de una corriente hidrocarbonada sensible a la temperatura.
JPS5470592A (en) Fender
ES2059798T3 (es) Nuevo catalizador que puede ser empleado en un procedimiento de reduccion selectiva de oxidos de nitrogeno.
CA2000015A1 (fr) Procede de reformage catalytique dans plusieurs zones reactionnelles a lit mobile cote a cote
CA2041905A1 (fr) Catalyseur de craquage de charges hydrocarbonees comprenant une zeolithe beta, une zeolithe y et une matrice
AR008431A1 (es) Procedimiento y dispositivo de craqueo catalitico en lecho fluidizado de una carga de hidrocarburos, poniendo en practica una zona en contacto mejorada.
MY128848A (en) Process for recovering homogeneous metal hydride catalysts
AU8466491A (en) Process for purifying high-temperature reducing gases
Muller et al. Adsorbate-Induced Surface Stress: Phonon Anomaly and Reconstruction on Ni (001) Surfaces
CN206859080U (zh) 一种用于连续箱梁桥施工用支撑装置
CN213656712U (zh) 一种新型除氧器
ES2148022A1 (es) Metodo y aparato para aplicar puntos de soldadura destinados a la soldadura de montaje de una armadura de viga de una grua
ES2076715T3 (es) Perfeccionamiento en los dispositivos de craqueo catalitico en estado fluido de cargas de hidrocarburos.
JPS5675289A (en) Low temperature liquefied-gas carrier with semi- independent tank
CN221501141U (zh) 一种改进的钢渣处理倾翻装置
JPS55136339A (en) Excavator
Davis Enimont Spends$ 215 M on TPEs
CN213622958U (zh) 一种起重机控制柜减震装置
CN214018493U (zh) 一种便于移动的医用包衣机

Legal Events

Date Code Title Description
FG2A Definitive protection

Ref document number: 479645

Country of ref document: ES