ES2075552T3 - Reactor y procedimiento para la realizacion de reacciones cataliticas heterogeneas en fase gaseosa. - Google Patents
Reactor y procedimiento para la realizacion de reacciones cataliticas heterogeneas en fase gaseosa.Info
- Publication number
- ES2075552T3 ES2075552T3 ES92115129T ES92115129T ES2075552T3 ES 2075552 T3 ES2075552 T3 ES 2075552T3 ES 92115129 T ES92115129 T ES 92115129T ES 92115129 T ES92115129 T ES 92115129T ES 2075552 T3 ES2075552 T3 ES 2075552T3
- Authority
- ES
- Spain
- Prior art keywords
- procedure
- reactor
- gaseous phase
- performing catalytic
- heterogeneous reactions
- 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
- 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
- B01J8/0207—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 flow within the bed being predominantly horizontal
- B01J8/0214—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 flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
-
- 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
- B01J8/0285—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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00141—Coils
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00203—Coils
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)
- Epoxy Compounds (AREA)
Abstract
LA SOLICITUD SE REFIERE A UN REACTOR Y A UN PROCEDIMIENTO PARA REALIZAR REACCIONES DE FASES GASEOSAS CATALITICAS HETEROGENEAS. EL PROCEDIMIENTO SE CARACTERIZA PORQUE LA MEZCLA DE REACCION CIRCULA A TRAVES DE UN MATERIAL SUELTO CATALIZADO (01) RADIALMENTE RESPECTO AL EJE LONGITUDINAL DEL REACTOR, Y PREFERENTEMENTE EN DIRECCION CENTRIPETA. OTRA CARACTERISTICA DEL PROCEDIMIENTO, SEGUN LA INVENCION, ES LA QUE EN EL MATERIAL CATALIZADO (01) SE HA INCORPORADO UN INTERCAMBIADOR DE CALOR (02) CON TUBOS ENROLLADOS, POR LOS CUALES FLUYE UN FLUIDO ABSORBENTE DE CALOR, PARA LA DISIPACION DE LA TEMPERATURA DE REACCION LIBERADA.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4131446A DE4131446A1 (de) | 1991-09-21 | 1991-09-21 | Reaktor und verfahren zur durchfuehrung heterogenkatalytischer gasphasenreaktionen |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2075552T3 true ES2075552T3 (es) | 1995-10-01 |
Family
ID=6441145
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES92115129T Expired - Lifetime ES2075552T3 (es) | 1991-09-21 | 1992-09-04 | Reactor y procedimiento para la realizacion de reacciones cataliticas heterogeneas en fase gaseosa. |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0534195B1 (es) |
JP (1) | JPH05261272A (es) |
DE (2) | DE4131446A1 (es) |
ES (1) | ES2075552T3 (es) |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
PT726929E (pt) * | 1994-09-02 | 2000-05-31 | Michael Grigorjewitsch Lapunow | Processo e reactor de reformacao catalitica |
DE19718871A1 (de) * | 1997-05-03 | 1998-11-12 | Krupp Uhde Gmbh | Verfahren zur Oxichlorierung von Ethylen in einem Wirbelschicht-Katalysatorbett |
DE19719375A1 (de) * | 1997-05-07 | 1998-11-12 | Linde Ag | Verfahren und Reaktor zur Herstellung von Ethylenoxid |
DE19849709C2 (de) * | 1998-10-28 | 2000-09-14 | Krupp Uhde Gmbh | Verfahren und Wirbelschicht-Reaktor zur Oxichlorierung von Ethylen, Sauerstoff und HCl |
EP1060788A1 (en) * | 1999-06-15 | 2000-12-20 | Methanol Casale S.A. | Isothermal catalytic reactor for exothermic or endothermic heterogeneous reactions |
DE19952964A1 (de) * | 1999-11-03 | 2001-05-10 | Basf Ag | Verfahren zur katalytischen Gasphasenoxidation zu (Meth)Acrolein und/oder (Meth)Acrylsäure |
IT1319549B1 (it) * | 2000-12-14 | 2003-10-20 | Methanol Casale Sa | Reattore per l'effettuazione di reazioni eterogenee esotermiche oendotermiche |
WO2003057653A1 (fr) | 2001-12-28 | 2003-07-17 | Mitsubishi Chemical Corporation | Procede d'oxydation catalytique en phase vapeur |
DE10235691B4 (de) * | 2002-07-31 | 2011-12-08 | Volkswagen Ag | Vorrichtung zum katalytischen Behandeln gasförmiger Medien |
DE10255294A1 (de) * | 2002-11-26 | 2004-06-03 | Basf Ag | Kontinuierliche Verfahren und Reaktor zur Herstellung von Alkylaminen |
EP1563900A1 (en) * | 2004-02-12 | 2005-08-17 | Methanol Casale S.A. | Pseudo-isothermal chemical reactor for heterogenous chemical reactions |
KR20070022160A (ko) | 2004-06-18 | 2007-02-23 | 바스프 악티엔게젤샤프트 | 메틸아민의 연속 합성 방법 |
DE102005059711A1 (de) | 2005-12-12 | 2007-06-14 | Basf Ag | Formkörper enthaltend ein mikroporöses Material und mindestens ein siliciumhaltiges Bindemittel, Verfahren zu seiner Herstellung und seine Verwendung als Katalysator, insbesondere in einem Verfahren zur kontinuierlichen Synthese von Methylaminen |
DE102008048526A1 (de) * | 2008-09-23 | 2010-04-01 | Uhde Gmbh | Verfahren zur Nutzung der im Herstellungsprozess von 1,2-Dichlorethan aus Ethylen in einem Wirbelschichtreaktor anfallenden Reaktionswärme |
CN102639227B (zh) * | 2009-12-01 | 2014-10-01 | 巴斯夫欧洲公司 | 用于进行自热气相脱氢的反应器 |
US20150224464A1 (en) * | 2014-02-13 | 2015-08-13 | Uop Llc | Radial flow reactor having a side inlet nozzle and methods for reacting hydrocarbons using the same |
CN105642197A (zh) * | 2014-09-24 | 2016-06-08 | 楼韧 | 一种大型反应器及其装置和工艺 |
JP2017536229A (ja) * | 2014-10-30 | 2017-12-07 | サビック グローバル テクノロジーズ ベスローテン フエンノートシャップ | 径方向に設置された冷却板を備えた反応器、及びそれを使用した方法 |
JP2017536445A (ja) | 2014-10-31 | 2017-12-07 | サビック グローバル テクノロジーズ ベスローテン フエンノートシャップ | 反応の軽質ガス状生成物からワックス生成物を分離するための反応器 |
CN109701456A (zh) * | 2019-03-12 | 2019-05-03 | 江苏永大化工机械有限公司 | 一种新型径向反应器 |
CN111250001A (zh) * | 2020-03-23 | 2020-06-09 | 江苏普格机械有限公司 | 高效变换炉 |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2363738A (en) * | 1939-08-05 | 1944-11-28 | Universal Oil Prod Co | Catalytic reactor |
JPS5839572B2 (ja) * | 1979-04-03 | 1983-08-31 | 東洋エンジニアリング株式会社 | 反応器およびその使用法 |
-
1991
- 1991-09-21 DE DE4131446A patent/DE4131446A1/de not_active Withdrawn
-
1992
- 1992-09-04 DE DE59203370T patent/DE59203370D1/de not_active Revoked
- 1992-09-04 EP EP92115129A patent/EP0534195B1/de not_active Revoked
- 1992-09-04 ES ES92115129T patent/ES2075552T3/es not_active Expired - Lifetime
- 1992-09-18 JP JP4249167A patent/JPH05261272A/ja not_active Withdrawn
Also Published As
Publication number | Publication date |
---|---|
JPH05261272A (ja) | 1993-10-12 |
DE59203370D1 (de) | 1995-09-28 |
DE4131446A1 (de) | 1993-06-09 |
EP0534195A1 (de) | 1993-03-31 |
EP0534195B1 (de) | 1995-08-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG2A | Definitive protection |
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