CL2012001053A1 - Proceso para producir etanol mediante la reducción del ácido acético que comprende el paso de ácido acético e hidrógeno sobre un catalizador que comprende platino y estaño sobre un soporte modificado con un modificador de soporte seleccionado de óxidos y metasilicatos de metal alcalino, alcalinotérreo, sus precursores y sus mezclas. - Google Patents
Proceso para producir etanol mediante la reducción del ácido acético que comprende el paso de ácido acético e hidrógeno sobre un catalizador que comprende platino y estaño sobre un soporte modificado con un modificador de soporte seleccionado de óxidos y metasilicatos de metal alcalino, alcalinotérreo, sus precursores y sus mezclas.Info
- Publication number
- CL2012001053A1 CL2012001053A1 CL2012001053A CL2012001053A CL2012001053A1 CL 2012001053 A1 CL2012001053 A1 CL 2012001053A1 CL 2012001053 A CL2012001053 A CL 2012001053A CL 2012001053 A CL2012001053 A CL 2012001053A CL 2012001053 A1 CL2012001053 A1 CL 2012001053A1
- Authority
- CL
- Chile
- Prior art keywords
- acetic acid
- support
- catalyst
- passage
- metasilicates
- Prior art date
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/36—Rhenium
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- B01J21/16—Clays or other mineral silicates
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- B01J23/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead
- B01J23/622—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead
- B01J23/626—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead with tin
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- B01J23/6522—Chromium
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- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
- C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
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- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—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 an oxygen containing functional group
- C07C29/136—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 an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/147—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 an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof
- C07C29/149—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 an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
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- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
Proceso para la producción de etanol mediante la reducción del ácido acético el cual comprende el paso de hidrógeno y ácido acético gaseoso sobre un catalizador que comprende Pt y Sn sobre un soporte modificado; y proceso para la hidrogenación de ácidos alcanoicos.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/588,727 US8309772B2 (en) | 2008-07-31 | 2009-10-26 | Tunable catalyst gas phase hydrogenation of carboxylic acids |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CL2012001053A1 true CL2012001053A1 (es) | 2012-12-14 |
Family
ID=42094265
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CL2012001052A CL2012001052A1 (es) | 2009-10-26 | 2012-04-25 | Proceso para producir etanol por hidrogenación de ácido acético en presencia de un catalizador que comprende un primer metal, un segundo metal, un soporte y un modificador de soporte seleccionado de oxidos y metasilicatos de metal alcalino, alcalino térreo, del grupo iib y iiib, y sus mezclas. |
| CL2012001053A CL2012001053A1 (es) | 2009-10-26 | 2012-04-25 | Proceso para producir etanol mediante la reducción del ácido acético que comprende el paso de ácido acético e hidrógeno sobre un catalizador que comprende platino y estaño sobre un soporte modificado con un modificador de soporte seleccionado de óxidos y metasilicatos de metal alcalino, alcalinotérreo, sus precursores y sus mezclas. |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CL2012001052A CL2012001052A1 (es) | 2009-10-26 | 2012-04-25 | Proceso para producir etanol por hidrogenación de ácido acético en presencia de un catalizador que comprende un primer metal, un segundo metal, un soporte y un modificador de soporte seleccionado de oxidos y metasilicatos de metal alcalino, alcalino térreo, del grupo iib y iiib, y sus mezclas. |
Country Status (7)
| Country | Link |
|---|---|
| US (4) | US8309772B2 (es) |
| KR (3) | KR20120086718A (es) |
| CN (1) | CN102557871B (es) |
| CL (2) | CL2012001052A1 (es) |
| CO (2) | CO6531474A2 (es) |
| RU (1) | RU2015104977A (es) |
| TW (1) | TWI525065B (es) |
Families Citing this family (197)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU2008226814C1 (en) | 2007-03-12 | 2014-11-20 | Intra-Cellular Therapies, Inc. | Substituted heterocycle fused gamma-carbolines synthesis |
| US8309773B2 (en) | 2010-02-02 | 2012-11-13 | Calanese International Corporation | Process for recovering ethanol |
| US8304586B2 (en) | 2010-02-02 | 2012-11-06 | Celanese International Corporation | Process for purifying ethanol |
| US7608744B1 (en) | 2008-07-31 | 2009-10-27 | Celanese International Corporation | Ethanol production from acetic acid utilizing a cobalt catalyst |
| US8338650B2 (en) | 2008-07-31 | 2012-12-25 | Celanese International Corporation | Palladium catalysts for making ethanol from acetic acid |
| US8680317B2 (en) * | 2008-07-31 | 2014-03-25 | Celanese International Corporation | Processes for making ethyl acetate from acetic acid |
| US8501652B2 (en) | 2008-07-31 | 2013-08-06 | Celanese International Corporation | Catalysts for making ethanol from acetic acid |
| US8546622B2 (en) | 2008-07-31 | 2013-10-01 | Celanese International Corporation | Process for making ethanol from acetic acid using acidic catalysts |
| US8471075B2 (en) * | 2008-07-31 | 2013-06-25 | Celanese International Corporation | Processes for making ethanol from acetic acid |
| US8309772B2 (en) | 2008-07-31 | 2012-11-13 | Celanese International Corporation | Tunable catalyst gas phase hydrogenation of carboxylic acids |
| US8637714B2 (en) | 2008-07-31 | 2014-01-28 | Celanese International Corporation | Process for producing ethanol over catalysts containing platinum and palladium |
| US7820852B2 (en) * | 2008-07-31 | 2010-10-26 | Celanese International Corporation | Direct and selective production of ethyl acetate from acetic acid utilizing a bimetal supported catalyst |
| US7863489B2 (en) * | 2008-07-31 | 2011-01-04 | Celanese International Corporation | Direct and selective production of ethanol from acetic acid utilizing a platinum/tin catalyst |
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| US8309772B2 (en) | 2008-07-31 | 2012-11-13 | Celanese International Corporation | Tunable catalyst gas phase hydrogenation of carboxylic acids |
| US7608744B1 (en) | 2008-07-31 | 2009-10-27 | Celanese International Corporation | Ethanol production from acetic acid utilizing a cobalt catalyst |
| US7863489B2 (en) * | 2008-07-31 | 2011-01-04 | Celanese International Corporation | Direct and selective production of ethanol from acetic acid utilizing a platinum/tin catalyst |
| EP2186787A1 (en) | 2008-11-13 | 2010-05-19 | BP p.l.c. | Hydrogenation of ethanoic acid to produce ethanol |
| US7884253B2 (en) * | 2008-12-11 | 2011-02-08 | Range Fuels, Inc. | Methods and apparatus for selectively producing ethanol from synthesis gas |
| US8450535B2 (en) | 2009-07-20 | 2013-05-28 | Celanese International Corporation | Ethanol production from acetic acid utilizing a cobalt catalyst |
| US8350098B2 (en) | 2011-04-04 | 2013-01-08 | Celanese International Corporation | Ethanol production from acetic acid utilizing a molybdenum carbide catalyst |
| CN102229520B (zh) | 2011-04-25 | 2013-12-11 | 江苏索普(集团)有限公司 | 一种由醋酸气相加氢制备乙醇的方法 |
| CN102228831A (zh) | 2011-04-25 | 2011-11-02 | 中国科学院大连化学物理研究所 | 一种乙酸气相加氢制取乙醇的催化剂 |
-
2009
- 2009-10-26 US US12/588,727 patent/US8309772B2/en not_active Expired - Fee Related
-
2010
- 2010-02-02 KR KR1020127013298A patent/KR20120086718A/ko not_active Withdrawn
- 2010-10-26 KR KR1020127013972A patent/KR20120082932A/ko not_active Withdrawn
- 2010-10-26 RU RU2015104977/04A patent/RU2015104977A/ru not_active Application Discontinuation
- 2010-10-26 CN CN201110452877.0A patent/CN102557871B/zh not_active Expired - Fee Related
- 2010-10-26 TW TW099136599A patent/TWI525065B/zh not_active IP Right Cessation
- 2010-10-26 KR KR1020127013399A patent/KR20120092135A/ko not_active Ceased
-
2011
- 2011-06-30 US US13/173,190 patent/US8080694B2/en not_active Expired - Fee Related
-
2012
- 2012-04-25 CL CL2012001052A patent/CL2012001052A1/es unknown
- 2012-04-25 CO CO12067982A patent/CO6531474A2/es not_active Application Discontinuation
- 2012-04-25 CL CL2012001053A patent/CL2012001053A1/es unknown
- 2012-04-25 CO CO12067984A patent/CO6531475A2/es not_active Application Discontinuation
- 2012-10-04 US US13/644,691 patent/US8754270B2/en not_active Expired - Fee Related
-
2014
- 2014-01-14 US US14/154,348 patent/US8993815B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| TWI525065B (zh) | 2016-03-11 |
| RU2015104977A (ru) | 2015-06-27 |
| CN102557871B (zh) | 2015-07-08 |
| KR20120086718A (ko) | 2012-08-03 |
| CN102557871A (zh) | 2012-07-11 |
| US8080694B2 (en) | 2011-12-20 |
| US8754270B2 (en) | 2014-06-17 |
| TW201139347A (en) | 2011-11-16 |
| US8309772B2 (en) | 2012-11-13 |
| US20130072728A1 (en) | 2013-03-21 |
| US20140128642A1 (en) | 2014-05-08 |
| KR20120082932A (ko) | 2012-07-24 |
| CO6531474A2 (es) | 2012-09-28 |
| CO6531475A2 (es) | 2012-09-28 |
| US20100121114A1 (en) | 2010-05-13 |
| US8993815B2 (en) | 2015-03-31 |
| CL2012001052A1 (es) | 2012-10-19 |
| KR20120092135A (ko) | 2012-08-20 |
| US20110263891A1 (en) | 2011-10-27 |
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