ES2159860T3 - Reactor para llevar a cabo reacciones de fase gaseosa/fase liquida/fase solida y un procedimiento para llevar a cabo estas reacciones usando dicho reactor. - Google Patents

Reactor para llevar a cabo reacciones de fase gaseosa/fase liquida/fase solida y un procedimiento para llevar a cabo estas reacciones usando dicho reactor.

Info

Publication number
ES2159860T3
ES2159860T3 ES97919772T ES97919772T ES2159860T3 ES 2159860 T3 ES2159860 T3 ES 2159860T3 ES 97919772 T ES97919772 T ES 97919772T ES 97919772 T ES97919772 T ES 97919772T ES 2159860 T3 ES2159860 T3 ES 2159860T3
Authority
ES
Spain
Prior art keywords
reaction chamber
phase
reactor
reactions
carry out
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
ES97919772T
Other languages
English (en)
Inventor
Albert Edward Jansen
Rob Klaassen
Heuven Jan Willem Van
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.)
Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO
Original Assignee
Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO
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 Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO filed Critical Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek TNO
Application granted granted Critical
Publication of ES2159860T3 publication Critical patent/ES2159860T3/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
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B01J10/007—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

LA INVENCION SE REFIERE A UN REACTOR PARA LLEVAR A CABO REACCIONES DE FASE GASEOSA/FASE LIQUIDA/FASE SOLIDA, QUE COMPRENDE UN ALOJAMIENTO (1) QUE ENCIERRA UNA CAMARA DE REACCION BASICAMENTE CERRADA (2) PARA CONTENER UNA PRIMERA FASE LIQUIDA, LA FASE SOLIDA Y UNA FASE GASEOSA (SUMINISTRADA A TRAVES DE LA CAMARA); AL MENOS UN DISPOSITIVO DE SUMINISTRO (3), CONECTADO A LA CAMARA DE REACCION, PARA SUMINISTRAR UNA PRIMERA FASE LIQUIDA A LA CAMARA DE REACCION (2); AL MENOS UNA FIBRA HUECA (4), CUYA PARED DEFINE UN CANAL DE FLUJO INTERNO PARA SEPARAR AL MENOS UNA SEGUNDA FASE LIQUIDA, DE FORMA QUE EL INTERCAMBIO DE MATERIAL TENGA LUGAR ENTRE LA CAMARA DE REACCION (2) Y EL CANAL DE FLUJO A TRAVES DE LA PARED DE LA FIBRA HUECA (4); AL MENOS UN CONDUCTO DE DESCARGA (6), CONECTADO AL CANAL DE FLUJO, PARA SEPARAR LA SEGUNDA FASE LIQUIDA; AL MENOS UN CONDUCTO DE ENTRADA DE GAS (7) Y AL MENOS UN CONDUCTO DE SALIDA DEL GAS (8), CONECTADOS A LA CAMARA DE REACCION (2) DE FORMA QUE, EN LA POSICION DE USO, ELCONDUCTO DE ENTRADA DEL GAS (7) SE ABRA ESENCIALMENTE HACIA EL FONDO DE LA CAMARA DE REACCION (2) Y EL CONDUCTO DE SALIDA DE GAS (8) SE SITUE BASICAMENTE EN LA PARTE SUPERIOR DE LA CAMARA DE REACCION (2), PARA SUMINISTRAR LA FASE GASEOSA ESENCIALMENTE EN LA DIRECCION ASCENDENTE A TRAVES DE LA CAMARA DE REACCION (2). LA INVENCION SE REFIERE ADEMAS A UN PROCEDIMIENTO PARA LLEVAR A CABO LAS REACCIONES DE FASE GASEOSA/FASE LIQUIDA/FASE SOLIDA, UTILIZANDO EL MENCIONADO REACTOR. LAS FIBRAS HUECA SON PREFERIBLEMENTE DE UN MATERIAL CERAMICO. EL REACTOR ES PREFERIBLEMENTE UN MODULO DAM Y/O ES ADECUADO PARA SU USO A TEMPERATURAS Y PRESIONES ELEVADAS.
ES97919772T 1996-05-03 1997-05-05 Reactor para llevar a cabo reacciones de fase gaseosa/fase liquida/fase solida y un procedimiento para llevar a cabo estas reacciones usando dicho reactor. Expired - Lifetime ES2159860T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL1003026A NL1003026C2 (nl) 1996-05-03 1996-05-03 Reactor voor het uitvoeren van gasfase/vloeistoffase/vaste fase reacties, alsmede een werkwijze voor het uitvoeren van dergelijke reacties onder toepassing van deze reactor.

Publications (1)

Publication Number Publication Date
ES2159860T3 true ES2159860T3 (es) 2001-10-16

Family

ID=19762797

Family Applications (1)

Application Number Title Priority Date Filing Date
ES97919772T Expired - Lifetime ES2159860T3 (es) 1996-05-03 1997-05-05 Reactor para llevar a cabo reacciones de fase gaseosa/fase liquida/fase solida y un procedimiento para llevar a cabo estas reacciones usando dicho reactor.

Country Status (9)

Country Link
US (1) US6245304B1 (es)
EP (1) EP0910464B1 (es)
JP (1) JP2000509645A (es)
AT (1) ATE203925T1 (es)
AU (1) AU2412897A (es)
DE (1) DE69706057T2 (es)
ES (1) ES2159860T3 (es)
NL (1) NL1003026C2 (es)
WO (1) WO1997041953A1 (es)

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US6461408B2 (en) * 1995-11-06 2002-10-08 Robert E. Buxbaum Hydrogen generator
CA2353307A1 (fr) 2001-07-13 2003-01-13 Carmen Parent Appareil et procede pour le traitement des effluents gazeux
CA2405635A1 (en) 2002-09-27 2004-03-27 C02 Solution Inc. A process and a plant for the production of useful carbonated species and for the recycling of carbon dioxide emissions from power plants
RU2397805C2 (ru) 2004-05-07 2010-08-27 Талеш Нанотецнологиаи Рт. Проточное лабораторное устройство для гидрирования и лабораторный способ гидрирования с использованием этого устройства
US8152999B2 (en) * 2004-05-21 2012-04-10 Wisconsin Alumni Research Foundation Membrane cascade-based separation
US10526299B2 (en) * 2004-12-22 2020-01-07 Chemtor, Lp Fiber conduit reactor with a heat exchange medium inlet and a heat exchange medium outlet
US9168469B2 (en) 2004-12-22 2015-10-27 Chemtor, Lp Method and system for production of a chemical commodity using a fiber conduit reactor
US8128825B2 (en) * 2004-12-22 2012-03-06 Chemtor, Lp Method and system for production of biofuels using a fiber conduit reactor
US7226883B1 (en) * 2006-06-05 2007-06-05 Merichem Chemicals & Refinery Services Llc Oxidizer and oxidation process for a desulphurization process
US9468866B2 (en) 2012-09-18 2016-10-18 Chemtor, Lp Use of a fiber conduit contactor for metal and/or metalloid extraction
EP3107651B1 (en) * 2014-02-20 2019-07-17 Spinchem AB Reactor arrangement and method of using such reactor arrangement
DE102015202681A1 (de) * 2015-02-13 2016-08-18 Friedrich-Alexander-Universität Erlangen-Nürnberg Verfahren zur Durchführung einer chemischen Synthese
DE102015202680A1 (de) * 2015-02-13 2016-08-18 Friedrich-Alexander-Universität Erlangen-Nürnberg Verfahren zur Durchführung einer chemischen Synthese und Synthesereaktor
DE102015215662A1 (de) * 2015-08-18 2017-02-23 Friedrich-Alexander-Universität Erlangen-Nürnberg Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen
DE102016204717A1 (de) * 2016-03-22 2017-09-28 Siemens Aktiengesellschaft Reaktor zur Durchführung von gleichgewichtslimitierten Reaktionen
DE102016204718A1 (de) 2016-03-22 2017-09-28 Siemens Aktiengesellschaft Reaktor

Family Cites Families (15)

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Publication number Priority date Publication date Assignee Title
JPS517488A (en) 1974-07-08 1976-01-21 Furukawa Electric Co Ltd Heikodensenno seizohoho
JPS531177A (en) * 1976-06-24 1978-01-07 Mitsui Eng & Shipbuild Co Ltd Gas-liquid contact reaction apparatus
US4789468A (en) * 1984-08-28 1988-12-06 The Trustees Of The Stevens Institute Of Technology Immobilized-interface solute-transfer apparatus
US5252220A (en) * 1989-09-25 1993-10-12 Symbiotech Incorporated Preparation of analytical samples by liquid-liquid extraction using microporous hollow-fiber membranes
NL9000014A (nl) * 1990-01-03 1991-08-01 Tno Overdrachtsmoduul voor het overdragen van stof en/of warmte van een mediumstroom naar een andere mediumstroom.
US5248424A (en) * 1990-08-17 1993-09-28 Zenon Environmental Inc. Frameless array of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
DE69316325T2 (de) * 1992-02-12 1998-05-28 Mitsubishi Rayon Co Hohlfasermembranemodul
GB9203958D0 (en) * 1992-02-25 1992-04-08 Norske Stats Oljeselskap Catalytic multi-phase reactor
DE4308697A1 (de) * 1993-03-18 1994-09-22 Durst Franz Prof Dr Dr H C Verfahren zur Anreicherung eines ersten gasförmigen oder flüssigen Mediums mit einem zweiten Gas oder einer zweiten Flüssigkeit sowie ein Reaktor zur Durchführung des Verfahrens
NL9302260A (nl) * 1993-12-24 1995-07-17 Stork Friesland Bv Membraan-bioreaktor met gas-lift systeem.
US5468283A (en) * 1994-07-21 1995-11-21 Transfair Corporation Hollow fiber membrane modules with transverse gas flow tailored for improved gas separation
US5614065A (en) * 1994-10-31 1997-03-25 Uop Distillation with membrane apparatus
CN1147210A (zh) * 1994-12-27 1997-04-09 有限会社米卡子基文化会馆 多孔陶瓷过滤器、其制造方法及多孔陶瓷过滤器制造用挤出成型模具和使用该模具的挤出成型装置
FR2734173B1 (fr) * 1995-05-19 1997-08-01 Rhone Poulenc Chimie Reacteur destine a la mise en oeuvre de reactions chimiques faisant intervenir une biomasse
US5932099A (en) * 1995-07-25 1999-08-03 Omnium De Traitements Et De Valorisation (Otv) Installation for biological water treatment for the production of drinkable water

Also Published As

Publication number Publication date
AU2412897A (en) 1997-11-26
ATE203925T1 (de) 2001-08-15
EP0910464A1 (en) 1999-04-28
US6245304B1 (en) 2001-06-12
NL1003026C2 (nl) 1997-11-06
WO1997041953A1 (en) 1997-11-13
EP0910464B1 (en) 2001-08-08
DE69706057T2 (de) 2001-11-22
DE69706057D1 (de) 2001-09-13
JP2000509645A (ja) 2000-08-02

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