AR087712A1 - Produccion de acido acetico con una alta proporcion de conversion - Google Patents
Produccion de acido acetico con una alta proporcion de conversionInfo
- Publication number
- AR087712A1 AR087712A1 ARP120103187A ARP120103187A AR087712A1 AR 087712 A1 AR087712 A1 AR 087712A1 AR P120103187 A ARP120103187 A AR P120103187A AR P120103187 A ARP120103187 A AR P120103187A AR 087712 A1 AR087712 A1 AR 087712A1
- Authority
- AR
- Argentina
- Prior art keywords
- acetic acid
- reactor
- carbon monoxide
- methanol
- conversion
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
- C07C51/12—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on an oxygen-containing group in organic compounds, e.g. alcohols
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Un proceso para obtener ácido acético que incluya los pasos de hacer reaccionar el monóxido de carbono y al menos uno de metanol y un derivado de metanol en un primer reactor sometido a las condiciones efectivas para obtener un producto de ácido acético sin tratar; separar el producto de ácido acético sin tratar en al menos una corriente derivada, al menos una de las corrientes derivadas contiene monóxido de carbono residual y haciendo reaccionar al menos una porción del monóxido de carbono residual con al menos un metanol y un derivado de metanol sobre el catalítico de metal en el segundo reactor para obtener ácido acético adicional. Preferentemente el segundo reactor es un reactor homogéneo y un reactor de monóxido de carbono de presión parcial menor a 1,05 MPa.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/368,880 US9663437B2 (en) | 2011-09-13 | 2012-02-08 | Production of acetic acid with high conversion rate |
Publications (1)
Publication Number | Publication Date |
---|---|
AR087712A1 true AR087712A1 (es) | 2014-04-09 |
Family
ID=46964015
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP120103187A AR087712A1 (es) | 2012-02-08 | 2012-08-29 | Produccion de acido acetico con una alta proporcion de conversion |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP2812305B1 (es) |
JP (1) | JP5995995B2 (es) |
CN (1) | CN103402965A (es) |
AR (1) | AR087712A1 (es) |
BR (1) | BR112013007324B1 (es) |
RS (1) | RS57932B1 (es) |
SG (1) | SG192556A1 (es) |
TW (1) | TW201332958A (es) |
WO (1) | WO2013119275A1 (es) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB201610338D0 (en) * | 2016-06-14 | 2016-07-27 | Bp Chem Int Ltd | Process |
WO2018135016A1 (ja) | 2017-01-18 | 2018-07-26 | 株式会社ダイセル | 酢酸の製造方法 |
WO2021186459A1 (en) * | 2020-03-16 | 2021-09-23 | Council Of Scientific And Industrial Research An Indian Registered Body Incorporated Under The Regn. Of Soc. Act (Act Xxi Of 1860) | An improved process for photocatalytic hydrocarboxylation of methanol with co2 to produce acetic acid |
CN114133324B (zh) * | 2021-12-06 | 2023-10-03 | 上海簇睿低碳能源技术有限公司 | 一种甲醇羰基化连续制备乙酸的方法和系统 |
Family Cites Families (41)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3769329A (en) | 1970-03-12 | 1973-10-30 | Monsanto Co | Production of carboxylic acids and esters |
US5144068A (en) | 1984-05-03 | 1992-09-01 | Hoechst Celanese Corporation | Methanol carbonylation process |
US5026908A (en) | 1984-05-03 | 1991-06-25 | Hoechst Celanese Corporation | Methanol carbonylation process |
US5001259A (en) | 1984-05-03 | 1991-03-19 | Hoechst Celanese Corporation | Methanol carbonylation process |
CA1299195C (en) | 1986-06-16 | 1992-04-21 | G. Paull Torrence | Addition of hydrogen to carbon monoxide feed gas in producing acetic acid by carbonylation of methanol |
DE3823645C1 (es) * | 1988-07-13 | 1989-11-30 | Hoechst Ag | |
DE9211421U1 (de) | 1992-08-25 | 1993-01-21 | TRW Repa GmbH, 7077 Alfdorf | Gassack-Rückhaltesystem für Fahrzeuge |
US5672743A (en) | 1993-09-10 | 1997-09-30 | Bp Chemicals Limited | Process for the production of acetic acid |
USRE35377E (en) | 1993-05-27 | 1996-11-12 | Steinberg; Meyer | Process and apparatus for the production of methanol from condensed carbonaceous material |
US5696284A (en) | 1995-06-21 | 1997-12-09 | Bp Chemicals Limited | Process for the carbonylation of alkyl alcohols and/or reactive derivatives thereof |
GB9517184D0 (en) * | 1995-08-22 | 1995-10-25 | Bp Chem Int Ltd | Process |
CN1092179C (zh) | 1995-10-27 | 2002-10-09 | 赫希斯特人造丝公司 | 除去腐蚀金属以改善羰基化催化剂溶液生产率的方法 |
IN192600B (es) | 1996-10-18 | 2004-05-08 | Hoechst Celanese Corp | |
US6339171B1 (en) | 1996-10-18 | 2002-01-15 | Celanese International Corporation | Removal or reduction of permanganate reducing compounds and alkyl iodides from a carbonylation process stream |
GB9625335D0 (en) * | 1996-12-05 | 1997-01-22 | Bp Chem Int Ltd | Process |
GB9626428D0 (en) | 1996-12-19 | 1997-02-05 | Bp Chem Int Ltd | Process |
GB9626317D0 (en) | 1996-12-19 | 1997-02-05 | Bp Chem Int Ltd | Process |
GB9626429D0 (en) | 1996-12-19 | 1997-02-05 | Bp Chem Int Ltd | Process |
US6627770B1 (en) | 2000-08-24 | 2003-09-30 | Celanese International Corporation | Method and apparatus for sequesting entrained and volatile catalyst species in a carbonylation process |
US6657078B2 (en) | 2001-02-07 | 2003-12-02 | Celanese International Corporation | Low energy carbonylation process |
US6617471B2 (en) | 2001-06-20 | 2003-09-09 | Eastman Chemical Company | Method for carbonylation of lower aliphatic alcohols using tin promoted iridium catalyst |
US7005541B2 (en) | 2002-12-23 | 2006-02-28 | Celanese International Corporation | Low water methanol carbonylation process for high acetic acid production and for water balance control |
US7223886B2 (en) | 2004-03-02 | 2007-05-29 | Celanese International Corporation | Removal of permanganate reducing compounds from methanol carbonylation process stream |
JP4526381B2 (ja) * | 2004-12-27 | 2010-08-18 | ダイセル化学工業株式会社 | 酢酸の製造方法 |
WO2007130724A2 (en) | 2006-02-06 | 2007-11-15 | Northwind Ventures | Systems and methods for volume reduction |
US7989659B2 (en) | 2007-05-17 | 2011-08-02 | Celanese International Corporation | Method and apparatus for making acetic acid with improved light ends column productivity |
US8017802B2 (en) | 2007-05-21 | 2011-09-13 | Celanese International Corporation | Control of impurities in reaction product of rhodium-catalyzed methanol carbonylation |
US8062482B2 (en) | 2007-10-30 | 2011-11-22 | Celanese International Corporation | Acetaldehyde removal from methyl acetate by distillation at elevated pressure |
EP2093209A1 (en) * | 2008-02-19 | 2009-08-26 | BP Chemicals Limited | Process for the production of acetic acid |
MY175851A (en) | 2008-04-29 | 2020-07-13 | Celanese Int Corp | Methanol carbonylation system having absorber with multiple solvent options |
US7820855B2 (en) * | 2008-04-29 | 2010-10-26 | Celanese International Corporation | Method and apparatus for carbonylating methanol with acetic acid enriched flash stream |
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 |
US8309773B2 (en) | 2010-02-02 | 2012-11-13 | Calanese International Corporation | Process for recovering ethanol |
US8471075B2 (en) | 2008-07-31 | 2013-06-25 | Celanese International Corporation | Processes for making ethanol from acetic acid |
US8338650B2 (en) | 2008-07-31 | 2012-12-25 | Celanese International Corporation | Palladium catalysts for making ethanol from acetic acid |
US7608744B1 (en) | 2008-07-31 | 2009-10-27 | Celanese International Corporation | Ethanol production from acetic acid utilizing a cobalt catalyst |
US8304586B2 (en) | 2010-02-02 | 2012-11-06 | Celanese International Corporation | Process for purifying ethanol |
US7884253B2 (en) | 2008-12-11 | 2011-02-08 | Range Fuels, Inc. | Methods and apparatus for selectively producing ethanol from synthesis gas |
US8318988B2 (en) | 2010-05-07 | 2012-11-27 | Celanese International Corporation | Process for purifying a crude ethanol product |
US8394988B2 (en) * | 2010-09-28 | 2013-03-12 | Celanese International Corporation | Production of acetic acid with high conversion rate |
US8877963B2 (en) * | 2010-09-28 | 2014-11-04 | Celanese International Corporation | Production of acetic acid with high conversion rate |
-
2012
- 2012-08-29 JP JP2014556532A patent/JP5995995B2/ja not_active Expired - Fee Related
- 2012-08-29 BR BR112013007324-1A patent/BR112013007324B1/pt not_active IP Right Cessation
- 2012-08-29 CN CN2012800034295A patent/CN103402965A/zh active Pending
- 2012-08-29 RS RS20181209A patent/RS57932B1/sr unknown
- 2012-08-29 EP EP12766745.9A patent/EP2812305B1/en not_active Not-in-force
- 2012-08-29 AR ARP120103187A patent/AR087712A1/es not_active Application Discontinuation
- 2012-08-29 TW TW101131370A patent/TW201332958A/zh unknown
- 2012-08-29 SG SG2013021449A patent/SG192556A1/en unknown
- 2012-08-29 WO PCT/US2012/052829 patent/WO2013119275A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
CN103402965A (zh) | 2013-11-20 |
EP2812305A1 (en) | 2014-12-17 |
SG192556A1 (en) | 2013-09-30 |
BR112013007324B1 (pt) | 2020-10-20 |
EP2812305B1 (en) | 2018-08-15 |
JP2015515446A (ja) | 2015-05-28 |
WO2013119275A1 (en) | 2013-08-15 |
BR112013007324A2 (pt) | 2016-07-05 |
RS57932B1 (sr) | 2019-01-31 |
JP5995995B2 (ja) | 2016-09-21 |
TW201332958A (zh) | 2013-08-16 |
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Legal Events
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FA | Abandonment or withdrawal |