MX2018002024A - Procedimiento para llevar a cabo reacciones limitadas por el equilibrio. - Google Patents
Procedimiento para llevar a cabo reacciones limitadas por el equilibrio.Info
- Publication number
- MX2018002024A MX2018002024A MX2018002024A MX2018002024A MX2018002024A MX 2018002024 A MX2018002024 A MX 2018002024A MX 2018002024 A MX2018002024 A MX 2018002024A MX 2018002024 A MX2018002024 A MX 2018002024A MX 2018002024 A MX2018002024 A MX 2018002024A
- Authority
- MX
- Mexico
- Prior art keywords
- reactor
- limited reactions
- sorbent
- equilibrium
- catalyst material
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract 4
- 238000006243 chemical reaction Methods 0.000 title abstract 2
- 239000003054 catalyst Substances 0.000 abstract 3
- 239000000463 material Substances 0.000 abstract 3
- 239000002594 sorbent Substances 0.000 abstract 3
- 238000001179 sorption measurement Methods 0.000 abstract 1
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
- B01J8/0278—Feeding reactive fluids
-
- 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
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/006—Separating solid material from the gas/liquid stream by filtration
-
- 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
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
-
- 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
- B01J8/222—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 in the presence of a rotating device only
-
- 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
- B01J8/224—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 the particles being subject to a circulatory movement
- B01J8/228—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 the particles being subject to a circulatory movement externally, i.e. the particles leaving the vessel and subsequently re-entering it
-
- 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
- B01J2208/00176—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles outside 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
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
-
- 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
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00292—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids
- B01J2208/003—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids involving reactant slurries
-
- 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
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00805—Details of the particulate material
- B01J2208/00814—Details of the particulate material the particulate material being provides in prefilled containers
-
- 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
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
-
- 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
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
- B01J2208/00902—Nozzle-type feeding elements
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)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Gas Separation By Absorption (AREA)
Abstract
La invención se refiere a un procedimiento para llevar a cabo reacciones limitadas por el equilibrio, que comprende las siguientes etapas: disponer un material catalizador en un reactor, incorporar eductos en el reactor, reacción de los eductos dando lugar a productos hasta alcanzar un estado de equilibrio, incorporar un agente de sorción en el reactor, sorción de los productos por el agente de sorción, el procedimiento se caracteriza por que el agente de sorción cargado con productos se acumula en una zona de acumulación en el reactor y por que el material catalizador está dispuesto en el reactor de modo que se separa de la zona de acumulación.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102015215662.1A DE102015215662A1 (de) | 2015-08-18 | 2015-08-18 | Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
| PCT/EP2016/066117 WO2017029024A1 (de) | 2015-08-18 | 2016-07-07 | Verfahren zur umsetzung von gleichgewichtslimitierten reaktionen |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MX2018002024A true MX2018002024A (es) | 2018-04-13 |
Family
ID=56418503
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX2018002024A MX2018002024A (es) | 2015-08-18 | 2016-07-07 | Procedimiento para llevar a cabo reacciones limitadas por el equilibrio. |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US10618021B2 (es) |
| EP (1) | EP3313564A1 (es) |
| JP (1) | JP6661005B2 (es) |
| KR (1) | KR102116731B1 (es) |
| CN (1) | CN107921395B (es) |
| AU (1) | AU2016309524B2 (es) |
| CL (1) | CL2018000369A1 (es) |
| DE (1) | DE102015215662A1 (es) |
| MA (1) | MA42252A (es) |
| MX (1) | MX2018002024A (es) |
| SA (1) | SA518390908B1 (es) |
| TN (1) | TN2018000053A1 (es) |
| WO (1) | WO2017029024A1 (es) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102015215662A1 (de) | 2015-08-18 | 2017-02-23 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
| DE102016204719A1 (de) * | 2016-03-22 | 2017-09-28 | Siemens Aktiengesellschaft | Reaktor |
| DE102017204226A1 (de) * | 2017-03-14 | 2018-09-20 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Mischung zur Verwendung als flüssiges Sorptionsmittel bei der Methanol-Synthese und Verfahren zur Methanol-Synthese unter Verwendung der Mischung |
| DE102017206763A1 (de) * | 2017-04-21 | 2018-10-25 | Siemens Aktiengesellschaft | Verfahren und Vorrichtung zum Umsetzen von Kohlenstoffdioxid zu Methanol |
| EP3556451B1 (de) * | 2018-04-20 | 2020-06-03 | Siemens Aktiengesellschaft | Verfahren zum betreiben einer reaktoranlage |
| ES3042614T3 (en) * | 2018-12-27 | 2025-11-21 | Vito Nv | A device and method for separating at least one reactant and at least one reaction product contained in a fluidic mixture |
| US20250033018A1 (en) * | 2020-11-23 | 2025-01-30 | Nitrocapt Ab | Thermal Reactor Comprising a Gas Permeable Cage Arranged to Influence a Flow Path of Gas |
| US20240293788A1 (en) * | 2021-06-10 | 2024-09-05 | Universiteit Antwerpen | Device and process set-up for equilibrium reactions |
| EP4230287A1 (en) * | 2022-02-16 | 2023-08-23 | Eidgenössische Materialprüfungs- und Forschungsanstalt | Sorption-enhanced catalytic reactors with thermal moderators |
Family Cites Families (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58146548A (ja) * | 1982-02-24 | 1983-09-01 | Asahi Chem Ind Co Ltd | ウレタンの製法 |
| GB2293334A (en) * | 1994-09-26 | 1996-03-27 | Shell Int Research Maatschappij B V | Process for carrying out chemical equilibrium reactions |
| US6303092B1 (en) | 1995-04-10 | 2001-10-16 | Air Products And Chemicals, Inc. | Process for operating equilibrium controlled reactions |
| DE69610134T2 (de) * | 1995-04-10 | 2001-01-11 | Air Products And Chemicals, Inc. | Verfahren zum Betreiben von gleichgewichtskontrollierten Reaktionen |
| NL1003026C2 (nl) * | 1996-05-03 | 1997-11-06 | Tno | Reactor voor het uitvoeren van gasfase/vloeistoffase/vaste fase reacties, alsmede een werkwijze voor het uitvoeren van dergelijke reacties onder toepassing van deze reactor. |
| JP2003221355A (ja) | 2002-01-25 | 2003-08-05 | Maruzen Petrochem Co Ltd | 環状ジアルデヒドの製造方法 |
| US6969505B2 (en) * | 2002-08-15 | 2005-11-29 | Velocys, Inc. | Process for conducting an equilibrium limited chemical reaction in a single stage process channel |
| US20040178124A1 (en) | 2003-03-11 | 2004-09-16 | Ke Liu | Hydrogen desulfurizer for hydrocarbon feeds with separated adsorption and catalyst material |
| JP2005015294A (ja) * | 2003-06-27 | 2005-01-20 | Toshiba Corp | 化学反応装置 |
| DE10361071A1 (de) | 2003-12-22 | 2005-07-14 | Basf Ag | Nitrilhydrierung in Gegenwart Ionischer Flüssigkeiten |
| DE102004008575A1 (de) | 2004-02-19 | 2005-09-08 | Stockhausen Gmbh | Spaltung oligomerer (Meth)acrylsäure in flüssiger Phase unter Druck |
| US20050229490A1 (en) * | 2004-04-19 | 2005-10-20 | Texaco Inc. | Reactor and apparatus for hydrogen generation |
| JP2005314500A (ja) | 2004-04-28 | 2005-11-10 | Mitsubishi Materials Corp | 高オクタン価ガソリン基材の製造方法 |
| EP2282828A2 (en) | 2008-04-09 | 2011-02-16 | Velocys, Inc. | Process for converting a carbonaceous material to methane, methanol and/or dimethyl ether using microchannel process technology |
| US20120029245A1 (en) * | 2009-03-17 | 2012-02-02 | Oberon Fuels, Inc. | Catalytic reactions using ionic liquids |
| CN102395527A (zh) * | 2009-03-27 | 2012-03-28 | 索尔维公司 | 生产过氧化氢的方法 |
| CL2010000726A1 (es) | 2010-07-07 | 2010-12-24 | Haldor Topsoe As | Metodo para preparar metanol que comprende hacer reaccionar un gas de sintesis en un reactor catalitico de lecho fijo de particulas de catalizador enfriadas indirectamente, y condensar metanol a medida que se forma sobre una superficie de enfriamiento; y reactor para realizar dicho metodo. |
| TWI428184B (zh) * | 2010-08-26 | 2014-03-01 | Atomic Energy Council | 提升漿態床反應器產率之方法 |
| CN102371136B (zh) * | 2010-12-08 | 2013-10-09 | 北京低碳清洁能源研究所 | 生产富含ch4气体的具有同轴闭合夹层结构的反应器系统以及使用该系统的方法 |
| CN104039699A (zh) | 2011-11-14 | 2014-09-10 | 森特瑟姆光伏美国有限公司 | 用于非平衡三氯氢硅制备的方法和系统 |
| JP6116383B2 (ja) | 2013-05-31 | 2017-04-19 | ユニ・チャーム株式会社 | 吸収性物品 |
| CN105175208B (zh) * | 2015-08-07 | 2017-11-14 | 北京华福工程有限公司 | 乙炔加氢制备乙烯的方法及用于该方法的反应塔 |
| DE102015215662A1 (de) | 2015-08-18 | 2017-02-23 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
-
2015
- 2015-08-18 DE DE102015215662.1A patent/DE102015215662A1/de not_active Withdrawn
-
2016
- 2016-07-07 CN CN201680048014.8A patent/CN107921395B/zh not_active Expired - Fee Related
- 2016-07-07 MA MA042252A patent/MA42252A/fr unknown
- 2016-07-07 WO PCT/EP2016/066117 patent/WO2017029024A1/de not_active Ceased
- 2016-07-07 AU AU2016309524A patent/AU2016309524B2/en not_active Ceased
- 2016-07-07 KR KR1020187007207A patent/KR102116731B1/ko not_active Expired - Fee Related
- 2016-07-07 MX MX2018002024A patent/MX2018002024A/es unknown
- 2016-07-07 JP JP2018508633A patent/JP6661005B2/ja not_active Expired - Fee Related
- 2016-07-07 EP EP16739436.0A patent/EP3313564A1/de not_active Withdrawn
- 2016-07-07 TN TNP/2018/000053A patent/TN2018000053A1/en unknown
- 2016-07-07 US US15/752,673 patent/US10618021B2/en not_active Expired - Fee Related
-
2018
- 2018-02-09 CL CL2018000369A patent/CL2018000369A1/es unknown
- 2018-02-12 SA SA518390908A patent/SA518390908B1/ar unknown
Also Published As
| Publication number | Publication date |
|---|---|
| SA518390908B1 (ar) | 2021-07-12 |
| US20180243713A1 (en) | 2018-08-30 |
| TN2018000053A1 (en) | 2019-07-08 |
| DE102015215662A1 (de) | 2017-02-23 |
| KR102116731B1 (ko) | 2020-05-29 |
| US10618021B2 (en) | 2020-04-14 |
| JP6661005B2 (ja) | 2020-03-11 |
| WO2017029024A1 (de) | 2017-02-23 |
| CN107921395B (zh) | 2021-06-18 |
| CN107921395A (zh) | 2018-04-17 |
| JP2018526203A (ja) | 2018-09-13 |
| AU2016309524B2 (en) | 2018-11-01 |
| MA42252A (fr) | 2018-05-02 |
| EP3313564A1 (de) | 2018-05-02 |
| CL2018000369A1 (es) | 2018-07-20 |
| KR20180039717A (ko) | 2018-04-18 |
| AU2016309524A1 (en) | 2018-03-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| MX2018002024A (es) | Procedimiento para llevar a cabo reacciones limitadas por el equilibrio. | |
| PH12013502162A1 (en) | Apparatuses, system and methods for forming pressed articles and pressed articles formed thereby | |
| MX369935B (es) | Sistema de reactor para la produccion de alotropos de carbono. | |
| MX2016004946A (es) | Procesos para la preparacion de compuestos plaguicidas. | |
| MX352037B (es) | Proceso de separacion con un sistema separador en caliente potenciado modificado. | |
| MX357222B (es) | Catalizador para la obtencion de alcoholes superiores. | |
| MX2018010305A (es) | Proceso para preparar terpinen-4-ol. | |
| WO2014127053A3 (en) | Process for ultra pure chemical production from biobased raw starting materials | |
| EP3189894A4 (en) | Catalyst for water-hydrogen exchange reaction, method for producing same and apparatus for water-hydrogen exchange reaction | |
| MX2016004485A (es) | Metodo para la produccion de compuestos fluorados. | |
| AP2013007151A0 (en) | Temperature control system, hydrocarbon synthesis reaction apparatus, hydrocarbon synthesis reaction system, and temperature control process | |
| ZA201305390B (en) | Catalyst recovery system, hydrocarbon synthesis reaction apparatus,hydrocarbon synthesis reaction system,and catalyst receovery process | |
| MX389335B (es) | Procedimiento de produccion de e-1-cloro-3,3,3-trifluoropropeno a partir de 1,1,3,3-tetracloropropeno. | |
| HUE057330T2 (hu) | Eljárás allulóz konverziós reakciótermék tisztítására | |
| SG10201809230YA (en) | Method for producing isobutylene from isobutanol | |
| SG11201507677VA (en) | Process for separating product gas using carbonylation processes | |
| MX2015011156A (es) | Procedimiento de fluoracion escalonado y sistema de reactores. | |
| IN2014DN07540A (es) | ||
| EP3170554A4 (en) | Catalyst for methanation reaction, method for producing catalyst for methanation reaction, and method for producing methane | |
| EA201691165A1 (ru) | Способ, включающий две реакционные зоны, и устройство для его осуществления | |
| EP3470136A4 (en) | CHEMICAL REACTION DEVICE AND PARTICLE MANUFACTURING METHOD USING THE CHEMICAL REACTION DEVICE | |
| WO2014141092A3 (en) | Improved process for the preparation of tenofovir | |
| MX366192B (es) | Nueva sintesis telescopica de 2-metoximetil-p-fenilenediamina. | |
| MY160047A (en) | Process for the preparation and work-up of a reaction mixture containing triacetone amine | |
| AP4062A (en) | Hydrocarbon synthesis reaction apparatus, start-up process thereof, and hydrocarbon synthesis reaction system |