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
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Physical Or Chemical Processes And Apparatus (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.
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) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
CN100569353C (zh) | 2004-05-07 | 2009-12-16 | 泰利斯纳米技术有限公司 | 流动型实验室氢化装置和使用该装置的实验室氢化方法 |
US8152999B2 (en) * | 2004-05-21 | 2012-04-10 | Wisconsin Alumni Research Foundation | Membrane cascade-based separation |
US8128825B2 (en) * | 2004-12-22 | 2012-03-06 | Chemtor, Lp | Method and system for production of biofuels using a fiber conduit reactor |
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 |
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 |
WO2015126291A1 (en) * | 2014-02-20 | 2015-08-27 | Nordic Chemquest Ab | An auxiliary reactor for biological or chemical transformation |
DE102015202680A1 (de) | 2015-02-13 | 2016-08-18 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Durchführung einer chemischen Synthese und Synthesereaktor |
DE102015202681A1 (de) * | 2015-02-13 | 2016-08-18 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Durchführung einer chemischen Synthese |
DE102015215662A1 (de) * | 2015-08-18 | 2017-02-23 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
DE102016204718A1 (de) | 2016-03-22 | 2017-09-28 | Siemens Aktiengesellschaft | Reaktor |
DE102016204717A1 (de) * | 2016-03-22 | 2017-09-28 | Siemens Aktiengesellschaft | Reaktor zur Durchführung von gleichgewichtslimitierten Reaktionen |
Family Cites Families (15)
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 |
WO1996020037A1 (fr) * | 1994-12-27 | 1996-07-04 | Yuugengaisya Mikazuki Bunkakaikan | Filtre poreux en ceramique, procede de fabrication dudit filtre, filiere de moulage par extrusion pour la fabrication dudit filtre et machine de moulage par extrusion utilisant ladite filiere |
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 |
-
1996
- 1996-05-03 NL NL1003026A patent/NL1003026C2/nl not_active IP Right Cessation
-
1997
- 1997-05-05 AU AU24128/97A patent/AU2412897A/en not_active Abandoned
- 1997-05-05 AT AT97919772T patent/ATE203925T1/de not_active IP Right Cessation
- 1997-05-05 DE DE69706057T patent/DE69706057T2/de not_active Expired - Lifetime
- 1997-05-05 WO PCT/NL1997/000253 patent/WO1997041953A1/en active IP Right Grant
- 1997-05-05 EP EP97919772A patent/EP0910464B1/en not_active Expired - Lifetime
- 1997-05-05 JP JP9539801A patent/JP2000509645A/ja active Pending
- 1997-05-05 ES ES97919772T patent/ES2159860T3/es not_active Expired - Lifetime
- 1997-05-05 US US09/180,190 patent/US6245304B1/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP0910464A1 (en) | 1999-04-28 |
AU2412897A (en) | 1997-11-26 |
EP0910464B1 (en) | 2001-08-08 |
US6245304B1 (en) | 2001-06-12 |
DE69706057D1 (de) | 2001-09-13 |
JP2000509645A (ja) | 2000-08-02 |
NL1003026C2 (nl) | 1997-11-06 |
ATE203925T1 (de) | 2001-08-15 |
WO1997041953A1 (en) | 1997-11-13 |
DE69706057T2 (de) | 2001-11-22 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG2A | Definitive protection |
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