MX2010008947A - Reactor para la preparacion de metanol. - Google Patents
Reactor para la preparacion de metanol.Info
- Publication number
- MX2010008947A MX2010008947A MX2010008947A MX2010008947A MX2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A MX 2010008947 A MX2010008947 A MX 2010008947A
- Authority
- MX
- Mexico
- Prior art keywords
- methanol
- reactor
- catalyst bed
- gaseous phase
- cooling surface
- Prior art date
Links
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title abstract 15
- 239000003054 catalyst Substances 0.000 abstract 4
- 230000003197 catalytic effect Effects 0.000 abstract 2
- 238000001816 cooling Methods 0.000 abstract 2
- 239000007792 gaseous phase Substances 0.000 abstract 2
- 238000009835 boiling Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- 239000002826 coolant Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000007791 liquid phase Substances 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
Classifications
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- 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
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
-
- 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
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
- B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
-
- 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
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- 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
- B01J8/0292—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 with stationary packing material in the bed, e.g. bricks, wire rings, baffles
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- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/065—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
- B01J8/02—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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling the reactor
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/152—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/04—Methanol
-
- 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
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- 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
- B01J2208/00123—Fingers
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- 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
- B01J2208/00132—Tubes
-
- 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
- B01J2208/0015—Plates; Cylinders
-
- 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
- B01J2208/00212—Plates; Jackets; Cylinders
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/0077—Baffles attached to the reactor wall inclined
- B01J2219/00772—Baffles attached to the reactor wall inclined in a helix
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
Un diseño mejorado de un reactor catalítico para la producción de metanol en condiciones de equilibrio, con lo cual el metanol a medida que se forma es separado de la fase gaseosa en la fase líquida dentro del reactor, sin reducir la actividad catalítica del catalizador de metanol. Esto se logra al ajustar el punto de ebullición de un agente de enfriamiento líquido que está en contacto indirecto con las partículas de catalizador y al proporcionar una relación específica del volumen del lecho de catalizador con respecto al área de la superficie de enfriamiento. Por esa razón, la condensación de metanol a medida que se forma en la fase gaseosa toma lugar en la superficie de enfriamiento dispuesta que está distribuida uniformemente dentro del reactor y dentro de una región muy limitada del lecho de catalizador. La figura más representativa de la invención es la número 1a.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DKPA200800261 | 2008-02-25 | ||
| DKPA200800260 | 2008-02-25 | ||
| PCT/EP2009/000972 WO2009106231A1 (en) | 2008-02-25 | 2009-02-12 | Reactor for the preparation of methanol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MX2010008947A true MX2010008947A (es) | 2010-09-07 |
Family
ID=40586790
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX2010008947A MX2010008947A (es) | 2008-02-25 | 2009-02-12 | Reactor para la preparacion de metanol. |
| MX2010007376A MX2010007376A (es) | 2008-02-25 | 2009-02-12 | Metodo y reactor para la preparacion de metanol. |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX2010007376A MX2010007376A (es) | 2008-02-25 | 2009-02-12 | Metodo y reactor para la preparacion de metanol. |
Country Status (17)
| Country | Link |
|---|---|
| US (3) | US8513314B2 (es) |
| EP (3) | EP2249958B1 (es) |
| JP (2) | JP2011515333A (es) |
| KR (2) | KR20100138884A (es) |
| CN (2) | CN101959586B (es) |
| AT (2) | ATE521407T1 (es) |
| AU (2) | AU2009218828B2 (es) |
| BR (2) | BRPI0907815B1 (es) |
| CA (2) | CA2713874C (es) |
| EA (2) | EA019311B1 (es) |
| ES (3) | ES2368027T3 (es) |
| MX (2) | MX2010008947A (es) |
| NZ (2) | NZ587453A (es) |
| PL (3) | PL2374533T3 (es) |
| RU (1) | RU2481151C2 (es) |
| WO (2) | WO2009106231A1 (es) |
| ZA (2) | ZA201004473B (es) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| EP2571612B1 (en) | 2010-05-20 | 2014-12-24 | Haldor Topsøe A/S | Method and apparatus for the separation of a liquid from a gas feed stream in a catalytic reactor |
| EA021500B1 (ru) | 2010-06-24 | 2015-06-30 | Хальдор Топсёэ А/С | Совместное производство метанола и аммиака |
| US20130153188A1 (en) * | 2011-12-16 | 2013-06-20 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Advanced smr reactor design featuring high thermal efficiency |
| EP3034161A1 (en) | 2014-12-18 | 2016-06-22 | Haldor Topsøe A/S | Method and reactor design for the production of methanol |
| DE102015202680A1 (de) | 2015-02-13 | 2016-08-18 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Durchführung einer chemischen Synthese und Synthesereaktor |
| RU2716797C2 (ru) * | 2015-07-15 | 2020-03-16 | Хальдор Топсёэ А/С | Каталитический реактор |
| US20180214837A1 (en) * | 2015-07-29 | 2018-08-02 | Primus Green Energy Inc. | Two-stage reactor for exothermal and reversible reactions and methods thereof |
| DK3400099T3 (da) | 2016-01-07 | 2020-06-02 | Total Raffinage Chimie | Fremgangsmåde til methanolsyntese under anvendelse af en indiumoxidbaseret katalysator |
| WO2017118572A1 (en) | 2016-01-07 | 2017-07-13 | Total Research & Technology Feluy | Supported indium oxide catalyst and process for methanol synthesis using the same |
| CN105797653A (zh) * | 2016-03-19 | 2016-07-27 | 江苏怡达化学股份有限公司 | 直接氧化法制备环氧丙烷的绿色合成反应装置及工艺 |
| 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 |
| CN108884008A (zh) * | 2016-03-30 | 2018-11-23 | 托普索公司 | 用于大生产容量的甲醇合成工艺布局 |
| EP3401300B1 (de) * | 2017-05-12 | 2021-06-23 | L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude | Verfahren zur herstellung von methanol |
| WO2018210827A1 (en) | 2017-05-17 | 2018-11-22 | Total Research & Technology Feluy | Mto-ocp upgrading process to maximize the selectivity to propylene |
| EP3404005A1 (en) | 2017-05-17 | 2018-11-21 | Total Research & Technology Feluy | Process for ethylene oligomerisation from diluted stream |
| WO2018210826A1 (en) | 2017-05-17 | 2018-11-22 | Total Research & Technology Feluy | Process for ethylene aromatisation from diluted stream |
| AR113649A1 (es) | 2017-12-20 | 2020-05-27 | Haldor Topsoe As | Convertidor de flujo axial enfriado |
| EP3593900A1 (en) | 2018-07-10 | 2020-01-15 | Total Raffinage Chimie | Copper-iron-based catalytic composition for the conversion of syngas to higher alcohols and process using such catalyst composition |
| EP3599075A1 (de) | 2018-07-27 | 2020-01-29 | Siemens Aktiengesellschaft | Reaktor zur durchführung einer chemischen gleichgewichtsreaktion |
| US11865519B2 (en) | 2018-09-06 | 2024-01-09 | Total Se | Noble metal-promoted IN2O3 catalyst for the hydrogenation of CO2 to methanol |
| US11306049B2 (en) | 2019-02-01 | 2022-04-19 | Total Se | Process using catalytic composition for the conversion of syngas to higher alcohols |
| EP3917669B1 (en) | 2019-02-01 | 2023-08-16 | TotalEnergies OneTech | Copper-iron-based catalytic composition comprising zeolites, method for producing such catalytic composition and process using such catalytic composition for the conversion of syngas to higher alcohols |
| CN114514068B (zh) * | 2019-08-27 | 2024-04-09 | 沙特基础工业全球技术公司 | 包括分配构件的传质旋流器 |
| CN114423516B (zh) | 2019-09-20 | 2024-11-22 | Sabic环球技术有限责任公司 | 反应器管组件 |
| CN114423515B (zh) * | 2019-09-27 | 2024-10-25 | 住友化学株式会社 | 化学反应方法及化学反应装置 |
| JP2021154230A (ja) * | 2020-03-27 | 2021-10-07 | 三菱パワー株式会社 | ガス状生成物を得るための装置およびガス状生成物を得るための方法 |
| EP4206173A4 (en) * | 2020-08-31 | 2024-09-18 | Sumitomo Chemical Company, Limited | CHEMICAL REACTION PROCESS, DEVICE FOR CHEMICAL REACTIONS AND MANUFACTURING PROCESS |
| WO2022045328A1 (ja) * | 2020-08-31 | 2022-03-03 | 住友化学株式会社 | メタノールの製造方法 |
| AU2021382100B2 (en) | 2020-11-17 | 2024-11-07 | Totalenergies Onetech | Process for methanol synthesis from co2-rich syngas |
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| CN114148553B (zh) * | 2021-11-12 | 2024-06-25 | 中国运载火箭技术研究院 | 一种类失重流体分布形态构建系统及控制系统 |
| CN115597405A (zh) * | 2022-10-11 | 2023-01-13 | 浙江软控智能科技有限公司(Cn) | 浆料高效冷却器 |
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| EP1080780B1 (en) * | 1999-08-31 | 2007-08-01 | Nippon Shokubai Co., Ltd. | Reactor for catalytic gas phase oxidation |
| US7132555B2 (en) * | 2000-09-26 | 2006-11-07 | Shell Oil Company | Rod-shaped inserts in reactor tubes |
| US20030068260A1 (en) * | 2001-03-05 | 2003-04-10 | Wellington Scott Lee | Integrated flameless distributed combustion/membrane steam reforming reactor and zero emissions hybrid power system |
| GB0116894D0 (en) * | 2001-07-11 | 2001-09-05 | Accentus Plc | Catalytic reactor |
| KR100440479B1 (ko) * | 2002-04-23 | 2004-07-14 | 주식회사 엘지화학 | 탄화수소의 열분해 공정 |
| GB0301323D0 (en) * | 2003-01-21 | 2003-02-19 | Johnson Matthey Plc | Methanol synthesis |
| US7161044B2 (en) * | 2003-10-22 | 2007-01-09 | Nippon Shokubai Co., Ltd. | Catalytic gas phase oxidation reaction |
| JP4487103B2 (ja) * | 2004-04-13 | 2010-06-23 | 財団法人北九州産業学術推進機構 | メタノールの高効率合成法及びそのための装置 |
| EP1600208A1 (en) * | 2004-05-24 | 2005-11-30 | Methanol Casale S.A. | Plate-type heat-exchanger |
| JP4967517B2 (ja) * | 2006-08-10 | 2012-07-04 | 株式会社Ihi | メタノール合成方法 |
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