MX2012004837A - Procesos para hacer etanol a partir de acido acetico. - Google Patents
Procesos para hacer etanol a partir de acido acetico.Info
- Publication number
- MX2012004837A MX2012004837A MX2012004837A MX2012004837A MX2012004837A MX 2012004837 A MX2012004837 A MX 2012004837A MX 2012004837 A MX2012004837 A MX 2012004837A MX 2012004837 A MX2012004837 A MX 2012004837A MX 2012004837 A MX2012004837 A MX 2012004837A
- Authority
- MX
- Mexico
- Prior art keywords
- acetic acid
- processes
- metal
- making ethanol
- rhenium
- Prior art date
Links
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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- 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
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/656—Manganese, technetium or rhenium
- B01J23/6567—Rhenium
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
- B01J37/0207—Pretreatment of the support
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
-
- 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
- C07C1/20—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
-
- 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
- C07C29/132—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
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/16—Clays or other mineral silicates
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- 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)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Un proceso de formación selectiva de etanol a partir de ácido acético por hidrogenación de ácido acético en presencia del primer metal, soporte silicáceo y al menos un modificador de soporte; preferentemente, el primer metal es seleccionado del grupo que consiste de cobre, hierro, cobalto, níquel, rutenio, rodio, paladio, osmio, iridio, platino, titanio, zinc, cromo, renio, molibdeno y tungsteno; además el catalizador puede constar de un segundo metal preferiblemente seleccionado del grupo que consiste en cobre, molibdeno, estaño, cromo, hierro, cobalto, vanadio, tungsteno, paladio, platino, lantano, cerio, manganeso, rutenio, renio, oro y níquel.
Applications Claiming Priority (2)
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 |
PCT/US2010/022947 WO2011053365A1 (en) | 2009-10-26 | 2010-02-02 | Processes for making ethanol from acetic acid |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2012004837A true MX2012004837A (es) | 2012-05-29 |
Family
ID=46506678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2012004837A MX2012004837A (es) | 2009-10-26 | 2010-02-02 | Procesos para hacer etanol a partir de acido acetico. |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP2493608A1 (es) |
JP (1) | JP2013508362A (es) |
CN (1) | CN102271805B (es) |
AU (1) | AU2010313767A1 (es) |
BR (1) | BR112012009825A2 (es) |
CA (1) | CA2777754A1 (es) |
HK (1) | HK1163589A1 (es) |
IL (1) | IL219398A0 (es) |
MX (1) | MX2012004837A (es) |
RU (1) | RU2012121861A (es) |
WO (1) | WO2011053365A1 (es) |
Families Citing this family (54)
Publication number | Priority date | Publication date | Assignee | Title |
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US8309773B2 (en) * | 2010-02-02 | 2012-11-13 | Calanese International Corporation | Process for recovering ethanol |
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 |
US8932372B2 (en) | 2010-02-02 | 2015-01-13 | Celanese International Corporation | Integrated process for producing alcohols from a mixed acid feed |
AU2011213125B2 (en) * | 2010-02-02 | 2014-07-17 | Celanese International Corporation | Process for purifying ethanol |
US8541633B2 (en) | 2010-02-02 | 2013-09-24 | Celanese International Corporation | Processes for producing anhydrous ethanol compositions |
WO2011097220A2 (en) * | 2010-02-02 | 2011-08-11 | Celanese International Corporation | Process for producing ethanol using an extractive distillation column |
US8552224B2 (en) | 2010-05-07 | 2013-10-08 | Celanese International Corporation | Processes for maximizing ethanol formation in the hydrogenation of acetic acid |
US8222466B2 (en) * | 2010-02-02 | 2012-07-17 | Celanese International Corporation | Process for producing a water stream from ethanol production |
US8858659B2 (en) | 2010-02-02 | 2014-10-14 | Celanese International Corporation | Processes for producing denatured ethanol |
CN102421521B (zh) * | 2010-02-02 | 2015-01-07 | 国际人造丝公司 | 用于生产乙醇的包含结晶载体改性剂的催化剂的制备和用途 |
WO2011097193A2 (en) * | 2010-02-02 | 2011-08-11 | Celanese International Corporation | Hydrolysis of ethyl acetate in ethanol separation process |
US8575403B2 (en) | 2010-05-07 | 2013-11-05 | Celanese International Corporation | Hydrolysis of ethyl acetate in ethanol separation process |
US8569551B2 (en) | 2010-05-07 | 2013-10-29 | Celanese International Corporation | Alcohol production process integrating acetic acid feed stream comprising water from carbonylation process |
US8680342B2 (en) | 2010-05-07 | 2014-03-25 | Celanese International Corporation | Process for recovering alcohol produced by hydrogenating an acetic acid feed stream comprising water |
US9024083B2 (en) | 2010-07-09 | 2015-05-05 | Celanese International Corporation | Process for the production of ethanol from an acetic acid feed and a recycled ethyl acetate feed |
US9272970B2 (en) | 2010-07-09 | 2016-03-01 | Celanese International Corporation | Hydrogenolysis of ethyl acetate in alcohol separation processes |
US8846988B2 (en) | 2010-07-09 | 2014-09-30 | Celanese International Corporation | Liquid esterification for the production of alcohols |
US9024085B2 (en) | 2011-04-26 | 2015-05-05 | Celanese International Corporation | Process to reduce ethanol recycled to hydrogenation reactor |
US9073816B2 (en) | 2011-04-26 | 2015-07-07 | Celanese International Corporation | Reducing ethyl acetate concentration in recycle streams for ethanol production processes |
US9000233B2 (en) | 2011-04-26 | 2015-04-07 | Celanese International Corporation | Process to recover alcohol with secondary reactors for hydrolysis of acetal |
US8907141B2 (en) | 2011-04-26 | 2014-12-09 | Celanese International Corporation | Process to recover alcohol with secondary reactors for esterification of acid |
US8927787B2 (en) | 2011-04-26 | 2015-01-06 | Celanese International Corporation | Process for controlling a reboiler during alcohol recovery and reduced ester formation |
US9000232B2 (en) | 2011-04-26 | 2015-04-07 | Celanese International Corporation | Extractive distillation of crude alcohol product |
US8927788B2 (en) | 2011-04-26 | 2015-01-06 | Celanese International Corporation | Process to recover alcohol with reduced water from overhead of acid column |
US9024084B2 (en) | 2011-04-26 | 2015-05-05 | Celanese International Corporation | Reduced energy alcohol separation process having controlled pressure |
US8884081B2 (en) | 2011-04-26 | 2014-11-11 | Celanese International Corporation | Integrated process for producing acetic acid and alcohol |
US9024082B2 (en) | 2011-04-26 | 2015-05-05 | Celanese International Corporation | Using a dilute acid stream as an extractive agent |
US8933278B2 (en) | 2011-04-26 | 2015-01-13 | Celanese International Corporation | Process for producing ethanol and reducing acetic acid concentration |
US8895786B2 (en) | 2011-08-03 | 2014-11-25 | Celanese International Corporation | Processes for increasing alcohol production |
US8877987B2 (en) | 2011-08-03 | 2014-11-04 | Celanese International Corportation | Process for producing anhydrous ethanol using extractive distillation column |
CN104010508B (zh) | 2011-10-05 | 2017-03-15 | 理辛德拉·N·博斯 | 用于大规模制备磷铂类抗肿瘤剂的高效方法 |
US8637715B2 (en) * | 2011-12-21 | 2014-01-28 | Celanese International Corporation | Catalysts comprising secondary noble metals and process for producing ethanol |
US9233899B2 (en) | 2011-12-22 | 2016-01-12 | Celanese International Corporation | Hydrogenation catalysts having an amorphous support |
CN103282333A (zh) * | 2011-12-22 | 2013-09-04 | 国际人造丝公司 | 使用具有无定形载体的加氢催化剂的乙醇方法 |
US9079172B2 (en) | 2012-03-13 | 2015-07-14 | Celanese International Corporation | Promoters for cobalt-tin catalysts for reducing alkanoic acids |
US9333496B2 (en) | 2012-02-29 | 2016-05-10 | Celanese International Corporation | Cobalt/tin catalyst for producing ethanol |
US8907142B2 (en) | 2011-12-29 | 2014-12-09 | Celanese International Corporation | Process for promoting catalyst activity for ethyl acetate conversion |
US8455702B1 (en) | 2011-12-29 | 2013-06-04 | Celanese International Corporation | Cobalt and tin catalysts for producing ethanol |
WO2013101305A1 (en) * | 2011-12-30 | 2013-07-04 | Celanese International Corporation | Pressure driven distillation for producing and recovering ethanol from hydrogenation process |
CN103874545B (zh) * | 2012-01-06 | 2016-08-24 | 国际人造丝公司 | 利用由多金属氧酸盐前体制备的加氢催化剂生产乙醇的方法 |
MX2014008252A (es) * | 2012-01-06 | 2014-08-08 | Celanese Int Corp | Catalizadores de hidrogenacion. |
US9051235B2 (en) | 2012-02-07 | 2015-06-09 | Celanese International Corporation | Process for producing ethanol using a molar excess of hydrogen |
US9050585B2 (en) | 2012-02-10 | 2015-06-09 | Celanese International Corporation | Chemisorption of ethyl acetate during hydrogenation of acetic acid to ethanol |
US8927786B2 (en) * | 2012-03-13 | 2015-01-06 | Celanese International Corporation | Ethanol manufacturing process over catalyst having improved radial crush strength |
US9073042B2 (en) | 2012-03-14 | 2015-07-07 | Celanese International Corporation | Acetic acid hydrogenation over a group VIII metal calcined catalyst having a secondary promoter |
US8975452B2 (en) | 2012-03-28 | 2015-03-10 | Celanese International Corporation | Process for producing ethanol by hydrocarbon oxidation and hydrogenation or hydration |
CN103787828B (zh) * | 2012-10-31 | 2015-10-07 | 中国石油化工股份有限公司 | 一种应用钴硼催化剂将羧酸气相加氢制备醇的方法 |
CN103787827B (zh) * | 2012-10-31 | 2015-10-07 | 中国石油化工股份有限公司 | 羧酸选择加氢制备醇的方法 |
CN103170352B (zh) * | 2013-03-28 | 2015-01-14 | 湖南长岭石化科技开发有限公司 | 一种乙酸仲丁酯加氢催化剂及其制备方法和应用 |
CN104117354A (zh) * | 2013-04-26 | 2014-10-29 | 中国科学院大连化学物理研究所 | 有机酸水相低温选择性加氢制备一元醇或二元醇的方法 |
CN103433039B (zh) * | 2013-09-11 | 2015-11-11 | 神华集团有限责任公司 | 一种醋酸酯加氢催化剂的制备方法 |
CN108358752A (zh) * | 2018-04-18 | 2018-08-03 | 肖锦 | 一种乙酸加氢制乙醇的方法 |
JP7342868B2 (ja) * | 2018-07-23 | 2023-09-12 | 三菱ケミカル株式会社 | アルコールの製造方法及び触媒 |
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US2882244A (en) | 1953-12-24 | 1959-04-14 | Union Carbide Corp | Molecular sieve adsorbents |
US3130007A (en) | 1961-05-12 | 1964-04-21 | Union Carbide Corp | Crystalline zeolite y |
US4398039A (en) * | 1981-05-18 | 1983-08-09 | The Standard Oil Company | Hydrogenation of carboxylic acids |
GB8509530D0 (en) | 1985-04-13 | 1985-05-15 | Bp Chem Int Ltd | Hydrogenation of carboxylic acids |
US5149680A (en) | 1987-03-31 | 1992-09-22 | The British Petroleum Company P.L.C. | Platinum group metal alloy catalysts for hydrogenation of carboxylic acids and their anhydrides to alcohols and/or esters |
GB8707595D0 (en) | 1987-03-31 | 1987-05-07 | British Petroleum Co Plc | Chemical process |
US5243095A (en) * | 1992-04-24 | 1993-09-07 | Engelhard Corporation | Hydrogenation catalyst, process for preparing and process for using said catalyst |
US5821111A (en) | 1994-03-31 | 1998-10-13 | Bioengineering Resources, Inc. | Bioconversion of waste biomass to useful products |
USRE35377E (en) | 1993-05-27 | 1996-11-12 | Steinberg; Meyer | Process and apparatus for the production of methanol from condensed carbonaceous material |
US5977010A (en) * | 1995-06-15 | 1999-11-02 | Engelhard Corporation | Shaped hydrogenation catalyst and processes for their preparation and use |
US6657078B2 (en) | 2001-02-07 | 2003-12-02 | Celanese International Corporation | Low energy carbonylation process |
US6685754B2 (en) | 2001-03-06 | 2004-02-03 | Alchemix Corporation | Method for the production of hydrogen-containing gaseous mixtures |
CN100537503C (zh) * | 2007-05-31 | 2009-09-09 | 上海华谊丙烯酸有限公司 | 一种甘油加氢制备正丙醇的方法 |
US7608744B1 (en) * | 2008-07-31 | 2009-10-27 | Celanese International Corporation | Ethanol production from acetic acid utilizing a cobalt catalyst |
-
2010
- 2010-02-02 CN CN201080003929.XA patent/CN102271805B/zh not_active Expired - Fee Related
- 2010-02-02 MX MX2012004837A patent/MX2012004837A/es not_active Application Discontinuation
- 2010-02-02 BR BR112012009825A patent/BR112012009825A2/pt not_active Application Discontinuation
- 2010-02-02 CA CA2777754A patent/CA2777754A1/en not_active Abandoned
- 2010-02-02 JP JP2012535196A patent/JP2013508362A/ja active Pending
- 2010-02-02 AU AU2010313767A patent/AU2010313767A1/en not_active Abandoned
- 2010-02-02 WO PCT/US2010/022947 patent/WO2011053365A1/en active Application Filing
- 2010-02-02 RU RU2012121861/04A patent/RU2012121861A/ru unknown
- 2010-02-02 EP EP10703399A patent/EP2493608A1/en not_active Withdrawn
-
2012
- 2012-04-24 IL IL219398A patent/IL219398A0/en unknown
- 2012-05-04 HK HK12104379.9A patent/HK1163589A1/xx not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
EP2493608A1 (en) | 2012-09-05 |
BR112012009825A2 (pt) | 2016-10-18 |
IL219398A0 (en) | 2012-06-28 |
HK1163589A1 (en) | 2012-09-14 |
AU2010313767A1 (en) | 2012-05-17 |
JP2013508362A (ja) | 2013-03-07 |
AU2010313767A2 (en) | 2012-07-26 |
CA2777754A1 (en) | 2011-05-05 |
WO2011053365A1 (en) | 2011-05-05 |
CN102271805B (zh) | 2014-07-09 |
CN102271805A (zh) | 2011-12-07 |
RU2012121861A (ru) | 2013-12-10 |
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Legal Events
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FA | Abandonment or withdrawal |