AR051075A1 - Proceso para uso en reacciones en fase gaseosa exotermicas en equilibrio. - Google Patents
Proceso para uso en reacciones en fase gaseosa exotermicas en equilibrio.Info
- Publication number
- AR051075A1 AR051075A1 ARP050103498A ARP050103498A AR051075A1 AR 051075 A1 AR051075 A1 AR 051075A1 AR P050103498 A ARP050103498 A AR P050103498A AR P050103498 A ARP050103498 A AR P050103498A AR 051075 A1 AR051075 A1 AR 051075A1
- Authority
- AR
- Argentina
- Prior art keywords
- stream
- gas
- final
- product
- phase
- Prior art date
Links
- 238000010574 gas phase reaction Methods 0.000 title abstract 4
- 238000000034 method Methods 0.000 title abstract 2
- 239000007789 gas Substances 0.000 abstract 16
- 239000000047 product Substances 0.000 abstract 9
- 239000007791 liquid phase Substances 0.000 abstract 6
- 239000012467 final product Substances 0.000 abstract 4
- 239000012071 phase Substances 0.000 abstract 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 2
- 238000006243 chemical reaction Methods 0.000 abstract 2
- 238000001816 cooling Methods 0.000 abstract 2
- 239000007792 gaseous phase Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 238000004064 recycling 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
- B01J8/04—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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/02—Preparation, purification or separation of ammonia
- C01C1/04—Preparation of ammonia by synthesis in the gas phase
- C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
- C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
- C07C1/0485—Set-up of reactors or accessories; Multi-step processes
-
- 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
- C07C29/1516—Multisteps
-
- 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
-
- 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)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Catalysts (AREA)
Abstract
Un proceso para uso en reacciones en fase gaseosa exotérmicas en equilibrio que comprende las etapas de: (a) proveer una corriente de reciclo con la adicion de gas de refresco, para formar una corriente de gas de alimentacion; (b) calentar la corriente de gas de alimentacion; (c) pasar la corriente de gas de alimentacion calentada a un primer reactor que contiene un catalizador para las reacciones en fase gaseosa exotérmicas, en condiciones adecuadas para la reaccion; (d) remover una corriente de producto que comprende producto y gases no reaccionados del primer reactor; (e) enfriar y condensar parcialmente la corriente de producto para formar una fase gaseosa y una fase líquida; (f) separar la fase líquida que contiene el producto deseado de la corriente de producto y remover dicha fase líquida; (g) separar la fase gaseosa de la corriente de producto para formar una corriente gaseosa; (h) opcionalmente mezclar la corriente gaseosa a partir de la corriente de producto con gas de refresco adicional; (i) calentar la corriente gaseosa; (j) pasar la corriente gaseosa calentada a un reactor final que contiene un catalizador para las reacciones en fase gaseosa exotérmicas en condiciones adecuadas para la reaccion; (k) remover una corriente de producto final que comprende producto y gases no reaccionados del reactor final; (l) enfriar y condensar parcialmente la corriente de producto final par formar una fase gaseosa final y una fase líquida final; (m) separar la fase líquida final que contiene el producto deseado desde la corriente de producto final y remover dicha fase líquida final y (n) separar la fase gaseosa de la corriente de producto final y reciclar el gas a la etapa (a), y en donde la corriente gaseosa de la etapa (g) es comprimida previamente al calentamiento en la etapa (i).
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB0418654.0A GB0418654D0 (en) | 2004-08-20 | 2004-08-20 | Process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AR051075A1 true AR051075A1 (es) | 2006-12-20 |
Family
ID=33042413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ARP050103498A AR051075A1 (es) | 2004-08-20 | 2005-08-19 | Proceso para uso en reacciones en fase gaseosa exotermicas en equilibrio. |
Country Status (16)
| Country | Link |
|---|---|
| US (1) | US7790775B2 (es) |
| EP (1) | EP1778610B1 (es) |
| CN (1) | CN1989092B (es) |
| AR (1) | AR051075A1 (es) |
| AT (1) | ATE455592T1 (es) |
| AU (1) | AU2005273687B2 (es) |
| BR (1) | BRPI0514433B1 (es) |
| DE (1) | DE602005019059D1 (es) |
| EA (1) | EA009834B1 (es) |
| EG (1) | EG24503A (es) |
| GB (1) | GB0418654D0 (es) |
| MY (1) | MY141554A (es) |
| NO (1) | NO338659B1 (es) |
| PL (1) | PL1778610T3 (es) |
| WO (1) | WO2006018610A1 (es) |
| ZA (1) | ZA200701478B (es) |
Families Citing this family (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102007040707B4 (de) * | 2007-08-29 | 2012-05-16 | Lurgi Gmbh | Verfahren und Anlage zur Herstellung von Methanol |
| DE102008049622B4 (de) * | 2008-09-30 | 2012-10-31 | Lurgi Gmbh | Verfahren und Anlage zur Herstellung von Methanol |
| DE102009034551A1 (de) * | 2009-07-23 | 2011-02-03 | Lurgi Gmbh | Verfahren und Anlage zur Herstellung von Methanol |
| CA2878964C (en) * | 2012-07-18 | 2019-05-28 | Haldor Topsoe A/S | Process and reaction system for the preparation of methanol |
| EP2818458B1 (en) * | 2013-06-27 | 2016-10-19 | Haldor Topsøe A/S | Process for the preparation of methanol in parallel reactors |
| CN106458804A (zh) * | 2014-06-20 | 2017-02-22 | 托普索公司 | 串联甲醇反应器 |
| DK3210961T3 (da) * | 2014-10-20 | 2021-05-03 | Mitsubishi Gas Chemical Co | Fremgangsmåde til fremstilling af methanol og indretning til fremstilling af methanol |
| EP3334704B1 (en) | 2015-08-12 | 2023-06-07 | Topsoe A/S | A novel process for methanol production from low quality synthesis gas |
| US20180370810A1 (en) * | 2015-12-16 | 2018-12-27 | Haldor Topsøe A/S | A process for production of ammonia from inert-free synthesis gas in multiple reaction systems |
| GB201600794D0 (en) * | 2016-01-15 | 2016-03-02 | Johnson Matthey Davy Technologies Ltd | Methanol process |
| GB201600793D0 (en) | 2016-01-15 | 2016-03-02 | Johnson Matthey Davy Technologies Ltd | Methanol process |
| EP3205622B1 (de) | 2016-02-11 | 2018-05-09 | Ulrich Wagner | Verfahren zur synthese von methanol |
| CN105753646B (zh) * | 2016-02-16 | 2017-11-21 | 南京国昌化工科技有限公司 | 一种节能型段间高低温梯度分醇两段产醇方法及装置 |
| EP3441381B1 (en) * | 2016-04-07 | 2020-05-13 | Mitsubishi Gas Chemical Company, Inc. | Method for producing methanol and device for producing methanol |
| CN106380376A (zh) * | 2016-11-25 | 2017-02-08 | 北京华福工程有限公司 | 合成系统和制备设备 |
| EP3336061A1 (en) * | 2016-12-14 | 2018-06-20 | Casale SA | A process for the synthesis of ammonia |
| DK3556451T3 (da) * | 2018-04-20 | 2020-08-31 | Siemens Ag | Fremgangsmåde til drift af et reaktoranlæg |
| MX2021001680A (es) * | 2018-08-17 | 2021-04-19 | Haldor Topsoe As | Un metodo para producir metanol en un reactor con derivacion. |
| GB201908449D0 (en) | 2019-06-12 | 2019-07-24 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
| GB201908450D0 (en) | 2019-06-12 | 2019-07-24 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
| EP3782973B1 (de) * | 2019-08-19 | 2023-03-01 | L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude | Verfahren und anlage zur herstellung von methanol |
| EP3808725A1 (de) * | 2019-10-16 | 2021-04-21 | L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude | Verfahren zum mehrstufigen herstellen von methanol |
| EP3808724A1 (de) * | 2019-10-16 | 2021-04-21 | L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude | Verfahren zum herstellen von methanol mittels mehrstufiger synthese |
| EP4015496B8 (de) * | 2020-12-15 | 2023-06-07 | L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Verfahren und anlage zum herstellen von methanol aus unterstöchiometrischem synthesegas |
| US20240140891A1 (en) | 2021-05-11 | 2024-05-02 | Johnson Matthey Davy Technologies Limited | Process for synthesising methanol |
| WO2022238671A1 (en) | 2021-05-11 | 2022-11-17 | Johnson Matthey Davy Technologies Limited | Process for synthesising methanol |
| GB2619796A (en) | 2022-05-09 | 2023-12-20 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
| GB202400240D0 (en) | 2024-01-08 | 2024-02-21 | Johnson Matthey Davy Technologies Ltd | Process for synthesising methanol |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US195219A (en) * | 1877-09-18 | Improvement in alarm-safes | ||
| US1868096A (en) | 1929-06-05 | 1932-07-19 | Dreyfus Henry | Manufacture of methyl alcohol |
| US1959219A (en) * | 1932-09-08 | 1934-05-15 | Forrest C Reed | Process of producing compounds containing carbon, hydrogen, and oxygen |
| FR2453125B1 (fr) | 1979-04-05 | 1985-06-07 | Inst Francais Du Petrole | Production d'alcools a partir de gaz de synthese |
| DE3518362A1 (de) * | 1985-05-22 | 1986-11-27 | Linde Ag, 6200 Wiesbaden | Verfahren zur herstellung von methanol |
| US4766154A (en) | 1987-02-06 | 1988-08-23 | Air Products And Chemicals, Inc. | Liquid phase methanol reactor staging process for the production of methanol |
| GB9023465D0 (en) | 1990-10-29 | 1990-12-12 | Shell Int Research | Process for the production of methanol |
| US5179129A (en) | 1991-03-01 | 1993-01-12 | Air Products And Chemicals, Inc. | Staged liquid phase methanol process |
| DE4416425A1 (de) * | 1994-05-10 | 1995-11-16 | Metallgesellschaft Ag | Verfahren zur Erzeugung von Methanol |
| GB9904649D0 (en) | 1998-05-20 | 1999-04-21 | Ici Plc | Methanol synthesis |
-
2004
- 2004-08-20 GB GBGB0418654.0A patent/GB0418654D0/en not_active Ceased
-
2005
- 2005-08-10 WO PCT/GB2005/003144 patent/WO2006018610A1/en active Application Filing
- 2005-08-10 EA EA200700326A patent/EA009834B1/ru not_active IP Right Cessation
- 2005-08-10 AT AT05794061T patent/ATE455592T1/de not_active IP Right Cessation
- 2005-08-10 ZA ZA200701478A patent/ZA200701478B/en unknown
- 2005-08-10 US US11/572,119 patent/US7790775B2/en active Active
- 2005-08-10 PL PL05794061T patent/PL1778610T3/pl unknown
- 2005-08-10 CN CN2005800245671A patent/CN1989092B/zh active Active
- 2005-08-10 AU AU2005273687A patent/AU2005273687B2/en active Active
- 2005-08-10 DE DE602005019059T patent/DE602005019059D1/de active Active
- 2005-08-10 BR BRPI0514433-7A patent/BRPI0514433B1/pt not_active IP Right Cessation
- 2005-08-10 EP EP05794061A patent/EP1778610B1/en active Active
- 2005-08-15 MY MYPI20053822A patent/MY141554A/en unknown
- 2005-08-19 AR ARP050103498A patent/AR051075A1/es not_active Application Discontinuation
-
2007
- 2007-02-11 EG EGNA2007000152 patent/EG24503A/xx active
- 2007-02-19 NO NO20070936A patent/NO338659B1/no unknown
Also Published As
| Publication number | Publication date |
|---|---|
| AU2005273687B2 (en) | 2010-09-16 |
| US20070225385A1 (en) | 2007-09-27 |
| BRPI0514433B1 (pt) | 2015-03-17 |
| CN1989092B (zh) | 2011-06-08 |
| ATE455592T1 (de) | 2010-02-15 |
| DE602005019059D1 (de) | 2010-03-11 |
| EA200700326A1 (ru) | 2007-06-29 |
| MY141554A (en) | 2010-05-14 |
| AU2005273687A1 (en) | 2006-02-23 |
| US7790775B2 (en) | 2010-09-07 |
| CN1989092A (zh) | 2007-06-27 |
| EA009834B1 (ru) | 2008-04-28 |
| PL1778610T3 (pl) | 2010-06-30 |
| NO338659B1 (no) | 2016-09-26 |
| EP1778610B1 (en) | 2010-01-20 |
| GB0418654D0 (en) | 2004-09-22 |
| EP1778610A1 (en) | 2007-05-02 |
| BRPI0514433A (pt) | 2008-06-10 |
| ZA200701478B (en) | 2008-04-30 |
| WO2006018610A1 (en) | 2006-02-23 |
| NO20070936L (no) | 2007-02-19 |
| EG24503A (en) | 2009-08-18 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG | Grant, registration | ||
| FD | Application declared void or lapsed, e.g., due to non-payment of fee |