MX2012008938A - Procedimiento para la produccion de etanol mediante la hidrogenacion de acido acetico vaporizado. - Google Patents
Procedimiento para la produccion de etanol mediante la hidrogenacion de acido acetico vaporizado.Info
- Publication number
- MX2012008938A MX2012008938A MX2012008938A MX2012008938A MX2012008938A MX 2012008938 A MX2012008938 A MX 2012008938A MX 2012008938 A MX2012008938 A MX 2012008938A MX 2012008938 A MX2012008938 A MX 2012008938A MX 2012008938 A MX2012008938 A MX 2012008938A
- Authority
- MX
- Mexico
- Prior art keywords
- acetic acid
- ethanol
- stream
- vapor feed
- feed stream
- 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
- C07C29/132—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
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
-
- 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
-
- 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
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
- C07C29/80—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by distillation
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Vaporización de ácido acético en presencia de hidrógeno para proporcionar una corriente de alimentación de vapor para un procedimiento de hidrogenación que produce etanol; el vaporizador forma una corriente de alimentación de vapor y una corriente de purga que tienen una relación en peso de la corriente de alimentación de vapor a la corriente del purga de por lo menos 2:1; el ácido acético puede vaporizarse a una temperatura debajo del punto de ebullición del ácido acético a la presión de trabajo del reactor; el procedimiento de hidrogenación produce un producto crudo de etanol y el etanol se separa del producto crudo; además, se puede separar también por lo menos una corriente de recirculación que comprende ácido acético y menos de 1.0% en peso de compuestos que tienen un punto de ebullición más alto que el del ácido acético; las corrientes de recirculación se pueden introducir al vaporizador junto con el ácido acético formar la corriente de alimentación de vapor.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US30081510P | 2010-02-02 | 2010-02-02 | |
US33269910P | 2010-05-07 | 2010-05-07 | |
US33269610P | 2010-05-07 | 2010-05-07 | |
US12/974,982 US8552225B2 (en) | 2010-02-02 | 2010-12-21 | Process for vaporizing acetic acid for hydrogenation processes to produce ethanol |
PCT/US2011/023332 WO2011097223A2 (en) | 2010-02-02 | 2011-02-01 | Process for vaporizing acetic acid for hydrogenation processes to produce ethanol |
Publications (1)
Publication Number | Publication Date |
---|---|
MX2012008938A true MX2012008938A (es) | 2012-08-15 |
Family
ID=44169138
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MX2012008938A MX2012008938A (es) | 2010-02-02 | 2011-02-01 | Procedimiento para la produccion de etanol mediante la hidrogenacion de acido acetico vaporizado. |
Country Status (16)
Country | Link |
---|---|
US (1) | US8552225B2 (es) |
EP (1) | EP2531472A2 (es) |
JP (1) | JP5792200B2 (es) |
KR (1) | KR20120115563A (es) |
CN (1) | CN102421732B (es) |
AU (1) | AU2011213062A1 (es) |
CA (1) | CA2787450A1 (es) |
CO (1) | CO6561810A2 (es) |
HK (1) | HK1169647A1 (es) |
MX (1) | MX2012008938A (es) |
NZ (1) | NZ601371A (es) |
RU (1) | RU2571425C2 (es) |
SG (1) | SG182692A1 (es) |
TW (1) | TW201139348A (es) |
WO (1) | WO2011097223A2 (es) |
ZA (1) | ZA201205234B (es) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
US9353034B2 (en) * | 2012-02-07 | 2016-05-31 | Celanese International Corporation | Hydrogenation process with reduced residence time for vapor phase reactants |
WO2013190853A1 (ja) | 2012-06-21 | 2013-12-27 | グリー株式会社 | ゲーム制御方法、ゲームサーバ、及びプログラム |
CN102908958B (zh) * | 2012-11-02 | 2015-10-28 | 江苏索普(集团)有限公司 | 一种由液相醋酸和氢气混合气化的方法 |
US8853469B2 (en) | 2012-11-20 | 2014-10-07 | Celanese International Corporation | Combined column for separating products of different hydrogenation reactors |
CN103894206B (zh) * | 2012-12-27 | 2016-09-07 | 中国石油化工股份有限公司 | 高活性铜基催化剂、制备方法及其用途 |
US10513715B2 (en) | 2015-09-24 | 2019-12-24 | Iogen Corporation | Wet oxidation of biomass |
CN106995363B (zh) * | 2016-01-25 | 2018-07-10 | 河南顺达化工科技有限公司 | 一种醋酸加氢耦合制备乙醇的工艺 |
CN109824479B (zh) * | 2019-04-10 | 2021-12-21 | 天津市汇筑恒升科技有限公司 | 乙二醇分离精制的节能及回收工艺 |
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-
2010
- 2010-12-21 US US12/974,982 patent/US8552225B2/en not_active Expired - Fee Related
-
2011
- 2011-02-01 TW TW100103899A patent/TW201139348A/zh unknown
- 2011-02-01 CN CN201180001961.9A patent/CN102421732B/zh not_active Expired - Fee Related
- 2011-02-01 EP EP11702905A patent/EP2531472A2/en not_active Withdrawn
- 2011-02-01 NZ NZ601371A patent/NZ601371A/en not_active IP Right Cessation
- 2011-02-01 WO PCT/US2011/023332 patent/WO2011097223A2/en active Application Filing
- 2011-02-01 AU AU2011213062A patent/AU2011213062A1/en not_active Abandoned
- 2011-02-01 SG SG2012054680A patent/SG182692A1/en unknown
- 2011-02-01 KR KR1020127022899A patent/KR20120115563A/ko active IP Right Grant
- 2011-02-01 CA CA2787450A patent/CA2787450A1/en not_active Abandoned
- 2011-02-01 RU RU2012137191/04A patent/RU2571425C2/ru not_active IP Right Cessation
- 2011-02-01 MX MX2012008938A patent/MX2012008938A/es active IP Right Grant
- 2011-02-01 JP JP2012551385A patent/JP5792200B2/ja not_active Expired - Fee Related
-
2012
- 2012-07-13 ZA ZA2012/05234A patent/ZA201205234B/en unknown
- 2012-07-17 CO CO12120081A patent/CO6561810A2/es not_active Application Discontinuation
- 2012-10-18 HK HK12110380.3A patent/HK1169647A1/xx not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
RU2012137191A (ru) | 2014-03-10 |
AU2011213062A1 (en) | 2012-08-02 |
RU2571425C2 (ru) | 2015-12-20 |
WO2011097223A3 (en) | 2011-11-03 |
KR20120115563A (ko) | 2012-10-18 |
CO6561810A2 (es) | 2012-11-15 |
CN102421732A (zh) | 2012-04-18 |
JP5792200B2 (ja) | 2015-10-07 |
US8552225B2 (en) | 2013-10-08 |
ZA201205234B (en) | 2013-09-25 |
US20110257442A1 (en) | 2011-10-20 |
WO2011097223A2 (en) | 2011-08-11 |
EP2531472A2 (en) | 2012-12-12 |
NZ601371A (en) | 2014-07-25 |
TW201139348A (en) | 2011-11-16 |
CN102421732B (zh) | 2014-06-25 |
CA2787450A1 (en) | 2011-08-11 |
HK1169647A1 (en) | 2013-02-01 |
JP2013518821A (ja) | 2013-05-23 |
SG182692A1 (en) | 2012-08-30 |
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