MXPA03004591A - Reactor de conversion quimica de carga con entradas de calor y circulacion cruzada de carga y de catalizador. - Google Patents

Reactor de conversion quimica de carga con entradas de calor y circulacion cruzada de carga y de catalizador.

Info

Publication number
MXPA03004591A
MXPA03004591A MXPA03004591A MXPA03004591A MXPA03004591A MX PA03004591 A MXPA03004591 A MX PA03004591A MX PA03004591 A MXPA03004591 A MX PA03004591A MX PA03004591 A MXPA03004591 A MX PA03004591A MX PA03004591 A MXPA03004591 A MX PA03004591A
Authority
MX
Mexico
Prior art keywords
feedstock
reactor
chemical conversion
circulation
heat inputs
Prior art date
Application number
MXPA03004591A
Other languages
English (en)
Inventor
Eric Lenglet
Original Assignee
Inst Francais Du Petrole
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 Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Publication of MXPA03004591A publication Critical patent/MXPA03004591A/es

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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • 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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0403—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal
    • B01J8/0423—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds
    • B01J8/0438—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds the beds being placed next to each other
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

La presente invencion se refiere a un reactor (R) de conversion quimica, que contiene entre un extremo superior y un extremo inferior un lecho catalitico (3a, 3b, 3c) sensiblemente vertical, y que comprende en combinacion: cerca de su extremo superior al menos un medio de introduccion de un catalizador solido (9), medios de introduccion (1) y evacuacion (2) de la carga que permiten su circulacion de manera sensiblemente horizontal a traves del lecho catalitico (3a, 3b, 3c), medios de calentamiento (4a, 4b) de la carga, integrados en el reactor (R) , el reactor ( R ) comprende cerca de su extremo inferior al menos un medio de extraccion diferenciado del catalizador (7a, 7b, 7c, 8a, 8b, 8c) entre una parte de corriente ascendente y una parte de corriente descendente del lecho catalitico (3a, 3b, 3c) relativamente en el sentido de circulacion de la carga.
MXPA03004591A 2000-11-29 2001-11-07 Reactor de conversion quimica de carga con entradas de calor y circulacion cruzada de carga y de catalizador. MXPA03004591A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0015426A FR2817172B1 (fr) 2000-11-29 2000-11-29 Reacteur de conversion chimique d'une charge avec apports de chaleur et circulation croisee de la charge et d'un catalyseur
PCT/FR2001/003458 WO2002043851A1 (fr) 2000-11-29 2001-11-07 Reacteur de conversion chimique d'une charge avec apports de chaleur et circulation croisee de la charge et d'un catalyseur

Publications (1)

Publication Number Publication Date
MXPA03004591A true MXPA03004591A (es) 2004-05-05

Family

ID=8857015

Family Applications (1)

Application Number Title Priority Date Filing Date
MXPA03004591A MXPA03004591A (es) 2000-11-29 2001-11-07 Reactor de conversion quimica de carga con entradas de calor y circulacion cruzada de carga y de catalizador.

Country Status (9)

Country Link
US (2) US20040067174A1 (es)
EP (1) EP1339483B1 (es)
JP (2) JP4875283B2 (es)
CA (1) CA2430246C (es)
DE (1) DE60110625T2 (es)
ES (1) ES2242790T3 (es)
FR (1) FR2817172B1 (es)
MX (1) MXPA03004591A (es)
WO (1) WO2002043851A1 (es)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101057155B (zh) * 2004-09-28 2012-03-28 昆士兰大学 磁场剂量仪
EP2334894A1 (en) * 2008-10-13 2011-06-22 Shell Oil Company Systems and methods of forming subsurface wellbores
JP6327888B2 (ja) * 2013-03-07 2018-05-23 新日鐵住金株式会社 石炭乾留ガスからの水素ガス製造装置および水素ガス製造方法
KR101831507B1 (ko) * 2016-01-05 2018-04-05 주식회사 효성 등온반응 유도용 자체 열공급 탈수소 반응기
KR101815750B1 (ko) * 2016-01-29 2018-01-31 주식회사 효성 탈수소 공정용 이동층 반응기
US11186784B2 (en) * 2018-10-15 2021-11-30 Uop Llc Dehydrogenation process having improved run time

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR877663A (fr) * 1940-12-11 1942-12-14 Metallgesellschaft Ag Dispositif pour effectuer des réactions catalytiques exothermiques
US2534859A (en) * 1946-04-18 1950-12-19 Socony Vacuum Oil Co Inc Method and apparatus for hydrocarbon conversion
US2865848A (en) * 1952-09-24 1958-12-23 Socony Mobil Oil Co Inc Temperature control in hydrocarbon conversion processes
DE2449789B1 (de) * 1974-10-19 1976-03-11 Deggendorfer Werft Eisenbau Mehrstufiger Horden-Reaktor
JPS5223572A (en) * 1975-08-15 1977-02-22 Sumitomo Chem Co Ltd Folded screen type reactor
JPS5260274A (en) * 1975-11-12 1977-05-18 Nippon Kokan Kk <Nkk> Solid-vapor contact apparatus
JPS57177330A (en) * 1981-04-27 1982-11-01 Babcock Hitachi Kk Apparatus for adsorbing sulfur dioxide
JPS59175442A (ja) * 1983-03-23 1984-10-04 Toyo Eng Corp メタンを含むガスの製造法
US4622210A (en) * 1984-08-13 1986-11-11 Standard Oil Company (Indiana) Sulfur oxide and particulate removal system
US5525311A (en) * 1994-05-02 1996-06-11 Uop Process and apparatus for controlling reaction temperatures
US5600052A (en) * 1994-05-02 1997-02-04 Uop Process and apparatus for controlling reaction temperatures
US5948240A (en) * 1997-11-17 1999-09-07 Uop Llc Process for controlling reaction temperatures
US6228341B1 (en) * 1998-09-08 2001-05-08 Uop Llc Process using plate arrangement for exothermic reactions
US6100436A (en) * 1998-09-08 2000-08-08 Uop Llc Process and apparatus for controlling reaction temperatures with heating arrangement in series flow
FR2821283B1 (fr) * 2001-02-28 2003-04-18 Inst Francais Du Petrole Procede et reacteur multi-etages catalytique a faible epaisseur avec echangeur thermique interne, et son utilisation

Also Published As

Publication number Publication date
FR2817172B1 (fr) 2003-09-26
US20040067174A1 (en) 2004-04-08
DE60110625D1 (de) 2005-06-09
US20060216218A1 (en) 2006-09-28
US7357855B2 (en) 2008-04-15
CA2430246A1 (fr) 2002-06-06
DE60110625T2 (de) 2005-11-10
EP1339483A1 (fr) 2003-09-03
JP2010051960A (ja) 2010-03-11
FR2817172A1 (fr) 2002-05-31
ES2242790T3 (es) 2005-11-16
WO2002043851A1 (fr) 2002-06-06
JP2004531361A (ja) 2004-10-14
EP1339483B1 (fr) 2005-05-04
CA2430246C (fr) 2009-10-13
JP4875283B2 (ja) 2012-02-15

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