MX2013004373A - Proceso y planta para la produccion de metanol por medio de lechos cataliticos isotermicos. - Google Patents
Proceso y planta para la produccion de metanol por medio de lechos cataliticos isotermicos.Info
- Publication number
- MX2013004373A MX2013004373A MX2013004373A MX2013004373A MX2013004373A MX 2013004373 A MX2013004373 A MX 2013004373A MX 2013004373 A MX2013004373 A MX 2013004373A MX 2013004373 A MX2013004373 A MX 2013004373A MX 2013004373 A MX2013004373 A MX 2013004373A
- Authority
- MX
- Mexico
- Prior art keywords
- gas
- methanol
- make
- catalytic beds
- plant
- Prior art date
Links
Classifications
-
- 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
- C07C29/32—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions without formation of -OH groups
-
- 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
- B01J8/04—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 passing successively through two or more beds
- B01J8/0446—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 passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—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 passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—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 passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- 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
- B01J8/04—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 passing successively through two or more beds
- B01J8/0446—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 passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—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 passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0457—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 passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being placed in separate reactors
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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
- B01J8/04—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 passing successively through two or more beds
- B01J8/0446—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 passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0461—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 passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds
- B01J8/0473—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 passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds the beds being placed in separate reactors
-
- 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
- B01J8/04—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 passing successively through two or more beds
- B01J8/0492—Feeding reactive fluids
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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
- B01J8/04—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 passing successively through two or more beds
- B01J8/0496—Heating or cooling the reactor
-
- 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
- C07C29/1512—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 reaction conditions
-
- 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
- B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
-
- 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
- B01J2219/00002—Chemical plants
- B01J2219/00004—Scale aspects
- B01J2219/00006—Large-scale industrial plants
-
- 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
- B01J2219/00002—Chemical plants
- B01J2219/00027—Process aspects
- B01J2219/0004—Processes in series
Abstract
Se describe un proceso para la síntesis de metanol que comprende Las etapas de reformar una fuente de hidrocarburo, obtener una alimentación de gas auxiliar (101), alimentar dicho gas auxiliar a un ciclo de síntesis (L), convertir dicho gas auxiliar en metanol (108) en un entorno catalítico sustancialmente isotérmico en donde dicho entorno catalítico comprende una pluralidad de lechos catalíticos isotérmicos (11, 12, 21) preferentemente dispuestos en serie, y al menos una porción del gas auxiliar (101) se mezcla con el gas de reciclo (112) del ciclo (L), obtener una mezcla gaseosa de gas fresco y gas de reciclo y al menos una porción de dicha mezcla gaseosa se dirige entre dos lechos catalíticos consecutivos que actúa como un gas de enfriamiento. También se divulga una planta asociada.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP10188537A EP2450100A1 (en) | 2010-10-22 | 2010-10-22 | Process and plant for the production of methanol with isothermal catalytic beds |
PCT/EP2011/063490 WO2012052204A1 (en) | 2010-10-22 | 2011-08-04 | Process and plant for the production of methanol with isothermal catalytic beds |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2013004373A true MX2013004373A (es) | 2013-05-22 |
Family
ID=43333328
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2013004373A MX2013004373A (es) | 2010-10-22 | 2011-08-04 | Proceso y planta para la produccion de metanol por medio de lechos cataliticos isotermicos. |
Country Status (9)
Country | Link |
---|---|
US (1) | US9040595B2 (es) |
EP (2) | EP2450100A1 (es) |
CN (1) | CN103180038B (es) |
AU (1) | AU2011317806A1 (es) |
BR (1) | BR112013009767A2 (es) |
CA (1) | CA2813517A1 (es) |
MX (1) | MX2013004373A (es) |
RU (1) | RU2564818C2 (es) |
WO (1) | WO2012052204A1 (es) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102015202680A1 (de) | 2015-02-13 | 2016-08-18 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Durchführung einer chemischen Synthese und Synthesereaktor |
DE102015208128A1 (de) * | 2015-04-30 | 2016-11-03 | Thyssenkrupp Ag | Asymmetrische Kreislaufkaskaden in der Gaskatalyse |
MY185748A (en) * | 2015-11-13 | 2021-06-03 | Johnson Matthey Plc | Apparatus and process for the production of formaldehyde |
GB201600793D0 (en) * | 2016-01-15 | 2016-03-02 | Johnson Matthey Davy Technologies Ltd | Methanol process |
EP3287432A1 (en) * | 2016-08-26 | 2018-02-28 | Casale SA | Process for methanol production |
EP4093536A1 (en) * | 2020-01-24 | 2022-11-30 | CRI, hf | Load-following reactor system, associated facilities, and method of operating the same |
EP4277736A1 (en) | 2021-01-15 | 2023-11-22 | Cri Hf | Methanol synthesis reactor |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5173513A (en) | 1980-09-04 | 1992-12-22 | Alwyn Pinto | Methanol synthesis |
CN1033267C (zh) * | 1991-07-09 | 1996-11-13 | 帝国化学工业公司 | 合成气的生产方法 |
EP0522744B1 (en) * | 1991-07-09 | 1997-08-13 | Imperial Chemical Industries Plc | Synthesis gas production |
DE19605572A1 (de) * | 1996-02-15 | 1997-08-21 | Metallgesellschaft Ag | Verfahren zum Erzeugen von Methanol |
GB9714744D0 (en) * | 1997-07-15 | 1997-09-17 | Ici Plc | Methanol |
DK173614B1 (da) * | 1999-02-02 | 2001-04-30 | Topsoe Haldor As | Fremgangsmåde til fremstilling af methanol/dimethyletherblanding fra syntesegas |
EP1153653A1 (en) | 2000-05-11 | 2001-11-14 | Methanol Casale S.A. | Reactor for exothermic or endothermic heterogeneous reactions |
EP1306126A1 (en) * | 2001-10-19 | 2003-05-02 | Methanol Casale S.A. | Heat exchange unit for isothermal chemical reactors |
RU2324674C1 (ru) * | 2006-12-27 | 2008-05-20 | Общество с ограниченной ответственностью "ЭСТ-Инвест" | Способ получения метанола |
DE102007040707B4 (de) * | 2007-08-29 | 2012-05-16 | Lurgi Gmbh | Verfahren und Anlage zur Herstellung von Methanol |
-
2010
- 2010-10-22 EP EP10188537A patent/EP2450100A1/en not_active Withdrawn
-
2011
- 2011-08-04 WO PCT/EP2011/063490 patent/WO2012052204A1/en active Application Filing
- 2011-08-04 US US13/880,495 patent/US9040595B2/en active Active
- 2011-08-04 CA CA2813517A patent/CA2813517A1/en not_active Abandoned
- 2011-08-04 AU AU2011317806A patent/AU2011317806A1/en not_active Abandoned
- 2011-08-04 CN CN201180050748.7A patent/CN103180038B/zh active Active
- 2011-08-04 EP EP11741459.9A patent/EP2629884B1/en active Active
- 2011-08-04 BR BR112013009767A patent/BR112013009767A2/pt not_active IP Right Cessation
- 2011-08-04 MX MX2013004373A patent/MX2013004373A/es active IP Right Grant
- 2011-08-04 RU RU2013123098/05A patent/RU2564818C2/ru active
Also Published As
Publication number | Publication date |
---|---|
AU2011317806A1 (en) | 2013-05-02 |
US9040595B2 (en) | 2015-05-26 |
RU2013123098A (ru) | 2014-11-27 |
EP2629884A1 (en) | 2013-08-28 |
CN103180038A (zh) | 2013-06-26 |
BR112013009767A2 (pt) | 2016-07-19 |
RU2564818C2 (ru) | 2015-10-10 |
EP2450100A1 (en) | 2012-05-09 |
EP2629884B1 (en) | 2015-06-17 |
US20130203872A1 (en) | 2013-08-08 |
CN103180038B (zh) | 2016-08-17 |
WO2012052204A1 (en) | 2012-04-26 |
CA2813517A1 (en) | 2012-04-26 |
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FG | Grant or registration |