ES8607752A1 - Una instalacion de reaccion de multiples etapas para efectu-ar contacto de flujo radial de una corriente de reaccion conparticulas de catalizador - Google Patents

Una instalacion de reaccion de multiples etapas para efectu-ar contacto de flujo radial de una corriente de reaccion conparticulas de catalizador

Info

Publication number
ES8607752A1
ES8607752A1 ES540703A ES540703A ES8607752A1 ES 8607752 A1 ES8607752 A1 ES 8607752A1 ES 540703 A ES540703 A ES 540703A ES 540703 A ES540703 A ES 540703A ES 8607752 A1 ES8607752 A1 ES 8607752A1
Authority
ES
Spain
Prior art keywords
stage reactor
reactor system
catalyst bed
moving catalyst
fed
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
Application number
ES540703A
Other languages
English (en)
Other versions
ES540703A0 (es
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.)
Honeywell UOP LLC
Original Assignee
UOP LLC
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 UOP LLC filed Critical UOP LLC
Publication of ES8607752A1 publication Critical patent/ES8607752A1/es
Publication of ES540703A0 publication Critical patent/ES540703A0/es
Expired 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
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor 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
    • 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
    • B01J8/125—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 with multiple sections one above the other separated by distribution aids, e.g. reaction and regeneration sections

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Meat, Egg Or Seafood Products (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
  • Liquid Crystal Substances (AREA)

Abstract

INSTALACION DE REACTOR DE MULTIPLES ETAPAS PARA EFECTUAR CONTACTO DE FLUJO RADIAL DE UNA CORRIENTE DE REACTIVO CON PARTICULAS DE CATALIZADOR. COMPRENDE: A) UNA CAMARA CERRADA ALARGADA VERTICALMENTE (1); B) DOS SECCIONES DE REACTOR (2, 3) ESPACIADAS, COMPRENDIENDO UNA DE LAS SECCIONES: A) UNA REJILLA INTERIOR (13) DE RETENCION DE CATALIZADOR DENTRO DE OTRA REJILLA (14); B) ELEMENTOS DE TABIQUE TRANSVERSAL (22) SUPERIOR; C) SEGUNDOS ELEMENTOS DE TABIQUE (29); D) ELEMENTOS DE TRANSFERENCIA DE CATALIZADOR (24) QUE COMPRENDEN: UN POZO (25); ELEMENTOS DE TABIQUE (16); SALIDAS (31) A LA ZONA (27); Y CONDUCTOS (12) DE TRANSFERENCIA; Y E) ELEMENTOS DE ENTRADA Y DE SALIDA DE CORRIENTE DE REACTIVO.
ES540703A 1984-02-27 1985-02-26 Una instalacion de reaccion de multiples etapas para efectu-ar contacto de flujo radial de una corriente de reaccion conparticulas de catalizador Expired ES8607752A1 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US06/584,207 US4567023A (en) 1984-02-27 1984-02-27 Multiple-stage reactor system for a moving catalyst bed
CN85103262A CN85103262B (zh) 1984-02-27 1985-04-27 带可移动催化剂床的多极反应器系统

Publications (2)

Publication Number Publication Date
ES8607752A1 true ES8607752A1 (es) 1986-06-01
ES540703A0 ES540703A0 (es) 1986-06-01

Family

ID=25741609

Family Applications (1)

Application Number Title Priority Date Filing Date
ES540703A Expired ES8607752A1 (es) 1984-02-27 1985-02-26 Una instalacion de reaccion de multiples etapas para efectu-ar contacto de flujo radial de una corriente de reaccion conparticulas de catalizador

Country Status (21)

Country Link
US (1) US4567023A (es)
EP (1) EP0154492B1 (es)
JP (1) JPS60209240A (es)
KR (1) KR890002150B1 (es)
CN (1) CN85103262B (es)
AT (1) ATE33947T1 (es)
AU (1) AU570300B2 (es)
CA (1) CA1219734A (es)
CS (1) CS247194B2 (es)
DD (1) DD239952A5 (es)
DE (1) DE3562459D1 (es)
DK (1) DK164356C (es)
ES (1) ES8607752A1 (es)
FI (1) FI80388C (es)
HU (1) HU197854B (es)
IN (1) IN160757B (es)
NO (1) NO163358C (es)
PT (1) PT80023B (es)
TR (1) TR22925A (es)
YU (1) YU44905B (es)
ZA (1) ZA851406B (es)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4567022A (en) * 1984-12-24 1986-01-28 Uop Inc. Apparatus for facilitating sampling of particulate matter passing from one treatment zone to another
US4923591A (en) * 1988-01-04 1990-05-08 Mobil Oil Corporation Continuous lubricating oil dewaxing process
US5209908A (en) * 1989-09-25 1993-05-11 Uop Radial flow reactor with double perforated scallops
US5366704A (en) * 1989-09-25 1994-11-22 Uop Radial flow reactor with double perforated scallops
US6117809A (en) * 1995-10-20 2000-09-12 Uop Llc Method for decreasing chloride emissions from a catalyst reduction process
US6884400B1 (en) 2001-06-22 2005-04-26 Uop Llc Reaction and regeneration system
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
CN100398190C (zh) * 2005-11-28 2008-07-02 中国石油化工集团公司 一种气固离心式移动床径向反应器
US7582268B1 (en) * 2006-07-12 2009-09-01 Uop Llc Reactor system with interstage product removal
US7622620B2 (en) * 2006-12-22 2009-11-24 Uop Llc Hydrocarbon conversion process including a staggered-bypass reaction system
CN101376092B (zh) * 2007-08-27 2010-05-19 中国石油化工股份有限公司 一种沸腾床反应器
US8324441B2 (en) * 2007-10-16 2012-12-04 Uop Llc Pentane catalytic cracking process
US7749467B2 (en) * 2007-12-18 2010-07-06 Uop Llc Optimizer hydraulic enhancement using milled plate
CN101367694B (zh) * 2008-09-18 2012-06-13 浙江大学 用于以含氧化合物为原料生产丙烯的卧式移动床反应器
DE102009019436A1 (de) 2009-04-29 2010-11-04 Bayer Materialscience Ag Verfahren zur Herstellung von aromatischen Aminen
FR3045405B1 (fr) * 2015-12-17 2018-01-26 IFP Energies Nouvelles Reacteur en lit mobile de faible capacite a ecoulement radial de la charge compose de plusieurs parties reliees par des brides
US10557091B2 (en) 2016-07-28 2020-02-11 Uop Llc Process for increasing hydrocarbon yield from catalytic reformer
FR3060414B1 (fr) * 2016-12-16 2019-01-25 IFP Energies Nouvelles Dispositif permettant le stockage temporaire et la remise en circulation d'une certaine quantite de catalyseur dans les unites de reformage catalytique.
WO2018148413A1 (en) * 2017-02-10 2018-08-16 Phillips 66 Company Configuring multiple catalytic beds
WO2020022934A1 (ru) * 2018-07-23 2020-01-30 Общество с ограниченной ответственностью "Институт по проектированию предприятий нефтеперерабатывающей и нефтехимической промышленности" (ООО "Ленгипронефтехим") Реактор с подвижным слоем катализатора
US10583412B1 (en) 2019-08-26 2020-03-10 Uop Llc Apparatus for catalytic reforming hydrocarbons having flow distributor and process for reforming hydrocarbons
US10933395B1 (en) 2019-08-26 2021-03-02 Uop Llc Apparatus for catalytic reforming hydrocarbons having flow distributor and process for reforming hydrocarbons
CN111848398B (zh) * 2020-07-14 2022-11-15 重庆市万利来化工股份有限公司 一种甲酸甲酯合成用脱氢反应装置及其工艺

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US23638A (en) * 1859-04-12 Improved mode of
US2518842A (en) * 1946-12-09 1950-08-15 Phillips Petroleum Co Means for securing even distribution of heated pebbles in the product heating chamber of a pebble furnace
US2818325A (en) * 1950-11-30 1957-12-31 Universal Oil Prod Co Apparatus for contacting subdivided solid particles in a compact and moving bed
US2897138A (en) * 1951-03-31 1959-07-28 Houdry Process Corp Contacting solids and gases
US2683654A (en) * 1952-01-25 1954-07-13 Universal Oil Prod Co Internally insulated and lined reactor
US3098815A (en) * 1957-03-21 1963-07-23 Sun Oil Co Process for regulating flow of contact material
US2997374A (en) * 1958-03-13 1961-08-22 California Research Corp Radial flow reactor
US2952623A (en) * 1958-04-30 1960-09-13 Sun Oil Co Controlling flow of granular solids
US3725248A (en) * 1969-09-25 1973-04-03 Universal Oil Prod Co Method of operating a reforming process
US3652231A (en) * 1969-09-25 1972-03-28 Universal Oil Prod Co Reconditioning system for moving column of reforming catalyst
US3692496A (en) * 1971-04-19 1972-09-19 Universal Oil Prod Co Apparatus for continuous reforming-regeneration process
US3706536A (en) * 1971-05-10 1972-12-19 Universal Oil Prod Co Multiple-stage stacked reactor system for moving bed catalyst particles
US3882015A (en) * 1973-05-29 1975-05-06 Universal Oil Prod Co Countercurrent catalytic contact of a reactant stream in a multi-stage process and the apparatus therefor
US3981824A (en) * 1974-11-13 1976-09-21 Universal Oil Products Company Regeneration method for gravity-flowing catalyst particles
US4110081A (en) * 1977-06-09 1978-08-29 Uop Inc. Moving-bed radial flow solids-fluid contacting apparatus
FR2427378A1 (fr) * 1978-05-29 1979-12-28 Inst Francais Du Petrole Appareil pour la conversion d'hydrocarbures
US4374095A (en) * 1981-10-29 1983-02-15 Chevron Research Company Method and apparatus for restraining radial flow catalytic reactor centerpipes
US4411869A (en) * 1981-12-28 1983-10-25 Uop Inc. Multiple stage reactor system
US4411870A (en) * 1981-12-28 1983-10-25 Uop Inc. Reactor system

Also Published As

Publication number Publication date
NO163358B (no) 1990-02-05
PT80023B (pt) 1987-06-17
ZA851406B (en) 1985-10-30
US4567023A (en) 1986-01-28
DK87185D0 (da) 1985-02-26
FI850776A0 (fi) 1985-02-26
CA1219734A (en) 1987-03-31
DK164356C (da) 1992-11-16
FI80388C (fi) 1990-06-11
CN85103262A (zh) 1986-10-22
CN85103262B (zh) 1988-10-12
NO850780L (no) 1985-08-28
YU44905B (en) 1991-04-30
AU570300B2 (en) 1988-03-10
EP0154492B1 (en) 1988-05-04
DD239952A5 (de) 1986-10-15
CS247194B2 (en) 1986-12-18
PT80023A (en) 1985-03-01
IN160757B (es) 1987-08-01
AU3903685A (en) 1985-09-05
EP0154492A2 (en) 1985-09-11
DK87185A (da) 1985-08-28
JPH0347135B2 (es) 1991-07-18
YU30685A (en) 1987-12-31
TR22925A (tr) 1988-11-28
JPS60209240A (ja) 1985-10-21
DE3562459D1 (en) 1988-06-09
EP0154492A3 (en) 1986-02-19
KR850006865A (ko) 1985-10-21
KR890002150B1 (ko) 1989-06-21
FI80388B (fi) 1990-02-28
DK164356B (da) 1992-06-15
FI850776L (fi) 1985-08-28
NO163358C (no) 1990-05-16
ES540703A0 (es) 1986-06-01
HU197854B (en) 1989-06-28
HUT42349A (en) 1987-07-28
ATE33947T1 (de) 1988-05-15

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Legal Events

Date Code Title Description
FD1A Patent lapsed

Effective date: 20050131