CL2009001003A1 - Proceso de carbonilacion para producir acido acetico que comprende carbonilar metanol, alimentar la mezcla de reaccion a un deposito de vaporizacion y calentar, donde la corriente de vapor del producto sin refinar conserva una temperatura superior a 148,88 grados celsius y la concentracion de acido acetico superior a 70% en peso. - Google Patents
Proceso de carbonilacion para producir acido acetico que comprende carbonilar metanol, alimentar la mezcla de reaccion a un deposito de vaporizacion y calentar, donde la corriente de vapor del producto sin refinar conserva una temperatura superior a 148,88 grados celsius y la concentracion de acido acetico superior a 70% en peso.Info
- Publication number
- CL2009001003A1 CL2009001003A1 CL2009001003A CL2009001003A CL2009001003A1 CL 2009001003 A1 CL2009001003 A1 CL 2009001003A1 CL 2009001003 A CL2009001003 A CL 2009001003A CL 2009001003 A CL2009001003 A CL 2009001003A CL 2009001003 A1 CL2009001003 A1 CL 2009001003A1
- Authority
- CL
- Chile
- Prior art keywords
- acetic acid
- feeding
- reaction mixture
- heating
- degrees celsius
- 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
-
- 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
- B01D3/06—Flash 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
- B01J14/00—Chemical processes in general for reacting liquids with liquids; Apparatus specially adapted therefor
- B01J14/005—Chemical processes in general for reacting liquids with liquids; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
- B01L3/00—Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
- B01L3/06—Crystallising dishes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
- C07C51/44—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
- C07C51/445—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation by steam distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C53/00—Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen
- C07C53/08—Acetic acid
-
- 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
-
- 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
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- 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
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00193—Sensing a parameter
- B01J2219/00195—Sensing a parameter of the reaction system
- B01J2219/00202—Sensing a parameter of the reaction system at the reactor outlet
-
- 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
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00211—Control algorithm comparing a sensed parameter with a pre-set value
- B01J2219/00213—Fixed parameter value
-
- 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
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00222—Control algorithm taking actions
- B01J2219/00227—Control algorithm taking actions modifying the operating conditions
- B01J2219/0024—Control algorithm taking actions modifying the operating conditions other than of the reactor or heat exchange system
-
- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/82—Metals of the platinum group
- B01J2531/822—Rhodium
-
- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/82—Metals of the platinum group
- B01J2531/827—Iridium
-
- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0231—Halogen-containing compounds
-
- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/20—Carbonyls
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Clinical Laboratory Science (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
Proceso; y aparato de carbonilación para producir ácido acético que comprende carbonilar metanol o sus derivados, alimentar la mezcla de reacción a un depósito de vaporización, calentar, la corriente de vapor del producto sin refinar conserva una temperatura superior a 148,88 grados celsius y una concentración de ácido acético superior a 70% peso.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/150,481 US7820855B2 (en) | 2008-04-29 | 2008-04-29 | Method and apparatus for carbonylating methanol with acetic acid enriched flash stream |
Publications (1)
Publication Number | Publication Date |
---|---|
CL2009001003A1 true CL2009001003A1 (es) | 2010-06-04 |
Family
ID=41018460
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CL2009001003A CL2009001003A1 (es) | 2008-04-29 | 2009-04-28 | Proceso de carbonilacion para producir acido acetico que comprende carbonilar metanol, alimentar la mezcla de reaccion a un deposito de vaporizacion y calentar, donde la corriente de vapor del producto sin refinar conserva una temperatura superior a 148,88 grados celsius y la concentracion de acido acetico superior a 70% en peso. |
Country Status (20)
Country | Link |
---|---|
US (7) | US7820855B2 (es) |
EP (2) | EP2323755B1 (es) |
JP (1) | JP5507544B2 (es) |
KR (1) | KR20110003555A (es) |
CN (1) | CN102015088B (es) |
AR (1) | AR074141A1 (es) |
AU (1) | AU2009241844A1 (es) |
BR (1) | BRPI0911487B1 (es) |
CA (1) | CA2721922C (es) |
CL (1) | CL2009001003A1 (es) |
DE (1) | DE09739136T1 (es) |
ES (2) | ES2694014T3 (es) |
HK (1) | HK1156560A1 (es) |
MX (3) | MX338852B (es) |
NZ (1) | NZ588701A (es) |
RU (1) | RU2508162C2 (es) |
SG (1) | SG190600A1 (es) |
TW (1) | TW200946493A (es) |
WO (1) | WO2009134333A1 (es) |
ZA (2) | ZA201007491B (es) |
Families Citing this family (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7820855B2 (en) | 2008-04-29 | 2010-10-26 | Celanese International Corporation | Method and apparatus for carbonylating methanol with acetic acid enriched flash stream |
KR101020844B1 (ko) * | 2008-09-04 | 2011-03-09 | 삼성전기주식회사 | 구리 나노입자의 저온 환원 소결을 위한 환원제 및 이를이용한 저온 소결 방법 |
CN102093198B (zh) * | 2009-12-15 | 2012-12-05 | 上海吴泾化工有限公司 | 一种生产乙酸的方法 |
CN102093196B (zh) * | 2009-12-15 | 2013-03-06 | 上海吴泾化工有限公司 | 一种链烷醇和/或其活性衍生物的羰基化制备羧酸的方法 |
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 |
US8637698B2 (en) * | 2010-11-19 | 2014-01-28 | Celanese International Corporation | Production of acetic acid with an increased production rate |
ES2646749T5 (es) | 2010-12-15 | 2021-10-21 | Daicel Corp | Procedimiento para producir ácido acético |
SG190940A1 (en) | 2010-12-15 | 2013-07-31 | Daicel Corp | Process for producing acetic acid |
US9663437B2 (en) | 2011-09-13 | 2017-05-30 | Celanese International Corporation | Production of acetic acid with high conversion rate |
JP5995995B2 (ja) * | 2012-02-08 | 2016-09-21 | セラニーズ・インターナショナル・コーポレーション | 高転化率での酢酸の製造 |
TWI547477B (zh) | 2012-03-14 | 2016-09-01 | 大賽璐股份有限公司 | 醋酸之製造方法 |
AR094541A1 (es) * | 2013-01-25 | 2015-08-12 | Daicel Corp | Procedimiento para producir ácido carboxílico |
US9340481B1 (en) | 2014-11-14 | 2016-05-17 | Celanese International Corporation | Process for flashing a reaction medium comprising lithium acetate |
MY181409A (en) * | 2014-11-14 | 2020-12-21 | Celanese Int Corp | Process for flashing a reaction medium comprising lithium acetate |
US9302975B1 (en) * | 2015-07-01 | 2016-04-05 | Celanese International Corporation | Process for flashing a reaction medium |
US9540303B2 (en) | 2015-04-01 | 2017-01-10 | Celanese International Corporation | Processes for producing acetic acid |
US9382183B1 (en) | 2015-07-01 | 2016-07-05 | Celanese International Corporation | Process for flashing a reaction medium |
US9382186B1 (en) | 2015-07-01 | 2016-07-05 | Celanese International Corporation | Process for producing acetic acid |
US9302974B1 (en) | 2015-07-01 | 2016-04-05 | Celanese International Corporation | Process for producing acetic acid |
US10428006B2 (en) * | 2015-09-30 | 2019-10-01 | Daicel Corporation | Method and apparatus for producing acetic acid |
US9416088B1 (en) | 2015-10-02 | 2016-08-16 | Celanese International Corporation | Process to produce acetic acid with recycle of water |
CN110114331A (zh) * | 2017-03-08 | 2019-08-09 | 株式会社大赛璐 | 乙酸的制备方法 |
US10457622B2 (en) | 2017-03-08 | 2019-10-29 | Daicel Corporation | Method for producing acetic acid |
US10308581B2 (en) | 2017-03-28 | 2019-06-04 | Daicel Corporation | Method for producing acetic acid |
MX2019011612A (es) | 2017-03-28 | 2019-11-18 | Daicel Corp | Metodo para producir acido acetico. |
CN111646894B (zh) * | 2019-09-10 | 2021-12-10 | 上海浦景化工技术股份有限公司 | 一种低压甲醇羰基化合成醋酸的方法 |
CN117120408B (zh) * | 2021-04-02 | 2024-05-07 | 利安德巴塞尔乙酰有限责任公司 | 用于生产乙酸的方法和系统 |
Family Cites Families (51)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3769329A (en) | 1970-03-12 | 1973-10-30 | Monsanto Co | Production of carboxylic acids and esters |
SU791735A1 (ru) * | 1977-07-27 | 1980-12-30 | Ереванский ордена Трудового Красного Знамени государственный университет | Способ очистки соли карбоновой кислоты |
NL8204901A (nl) | 1981-12-30 | 1983-07-18 | Halcon Sd Group Inc | Zuivering van carbonyleringsprodukten. |
US5001259A (en) | 1984-05-03 | 1991-03-19 | Hoechst Celanese Corporation | Methanol carbonylation process |
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 |
EP0391680B1 (en) * | 1989-04-06 | 1994-06-15 | BP Chemicals Limited | Process for preparing carboxylic acids |
US4976947A (en) * | 1990-02-20 | 1990-12-11 | Eastman Kodak Company | Process for the recovery of elemental iodine from alkyl iodides |
GB9120902D0 (en) * | 1991-10-02 | 1991-11-13 | Bp Chem Int Ltd | Purification process |
US5334755A (en) | 1992-04-24 | 1994-08-02 | Chiyoda Corporation | Process for the production of acetic acid from methanol and carbon monoxide using supported rhodium catalyst |
GB9211671D0 (en) * | 1992-06-02 | 1992-07-15 | Bp Chem Int Ltd | Process |
CN1043525C (zh) | 1992-08-13 | 1999-06-02 | 化学工业部西南化工研究院 | 甲醇低压液相羰基合成醋酸反应方法 |
US5672743A (en) | 1993-09-10 | 1997-09-30 | Bp Chemicals Limited | Process for the production of acetic acid |
GB9306409D0 (en) | 1993-03-26 | 1993-05-19 | Bp Chem Int Ltd | Process |
US5990347A (en) | 1993-03-26 | 1999-11-23 | Bp Chemicals Limited | Process for preparing a carboxylic acid |
US5352415A (en) | 1993-09-29 | 1994-10-04 | Hoechst Celanese Corporation | Control system for acetic acid manufacturing process |
JP3308392B2 (ja) * | 1994-06-02 | 2002-07-29 | ダイセル化学工業株式会社 | カルボニル化反応方法 |
JP3306227B2 (ja) | 1994-07-06 | 2002-07-24 | ダイセル化学工業株式会社 | 酢酸および/または無水酢酸の製造法 |
JP3413536B2 (ja) | 1994-06-20 | 2003-06-03 | 石川島播磨重工業株式会社 | 液圧駆動型水中音源装置 |
FR2726556B1 (fr) | 1994-11-04 | 1996-12-20 | Rhone Poulenc Chimie | Procede de preparation d'acides carboxyliques par carbonylation en presence d'iridium |
GB9503385D0 (en) * | 1995-02-21 | 1995-04-12 | Bp Chem Int Ltd | Process |
JP3927237B2 (ja) * | 1995-04-27 | 2007-06-06 | ダイセル化学工業株式会社 | 酢酸の製造法 |
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 |
AU702225B2 (en) * | 1995-10-27 | 1999-02-18 | Hoechst Celanese Corporation | Process for improving productivity of a carbonylation catalyst solution by removing corrosion metals |
IN192600B (es) | 1996-10-18 | 2004-05-08 | Hoechst Celanese Corp | |
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 |
GB9626324D0 (en) | 1996-12-19 | 1997-02-05 | Bp Chem Int Ltd | Process |
US6066762A (en) | 1996-12-30 | 2000-05-23 | Chiyoda Corporation | Process for the production of carbonyl compound |
US6153792A (en) | 1997-12-18 | 2000-11-28 | Uop Llc | Carbonylation process using a flash step with washing |
US6114576A (en) | 1997-12-18 | 2000-09-05 | Uop Llc | Carbonylation process with integrated heat exchange |
JP4242952B2 (ja) | 1998-08-31 | 2009-03-25 | ダイセル化学工業株式会社 | 酢酸の製造方法 |
US6552221B1 (en) | 1998-12-18 | 2003-04-22 | Millenium Petrochemicals, Inc. | Process control for acetic acid manufacture |
US6221405B1 (en) | 1999-05-11 | 2001-04-24 | Jac Pac Foods, Ltd. | Method of bonding and tenderizing meat |
US6303813B1 (en) | 1999-08-31 | 2001-10-16 | Celanese International Corporation | Rhodium/inorganic iodide catalyst system for methanol carbonylation process with improved impurity profile |
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 |
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 |
JP4489487B2 (ja) | 2004-04-02 | 2010-06-23 | ダイセル化学工業株式会社 | ヨウ化水素の分離方法 |
JP4732743B2 (ja) | 2004-12-06 | 2011-07-27 | ダイセル化学工業株式会社 | 蒸留方法 |
US7855306B2 (en) | 2005-04-28 | 2010-12-21 | Celanese International Corporation | Process for the production of acetic acid |
EP2093209A1 (en) * | 2008-02-19 | 2009-08-26 | BP Chemicals Limited | Process for the production of acetic acid |
US7820855B2 (en) * | 2008-04-29 | 2010-10-26 | Celanese International Corporation | Method and apparatus for carbonylating methanol with acetic acid enriched flash stream |
CN102131758A (zh) | 2008-06-28 | 2011-07-20 | Aa保费投资公司 | 用于生产羧酸的组合物及其制备方法和使用方法 |
US7790920B2 (en) | 2008-09-11 | 2010-09-07 | Lyondell Chemical Technology, L.P. | Preparation of acetic acid |
US8637699B2 (en) | 2011-04-15 | 2014-01-28 | Lyondell Chemical Technology, L.P. | Process for the manufacture of acetic acid |
JP5802550B2 (ja) | 2011-12-28 | 2015-10-28 | 株式会社東芝 | 水位計測装置 |
TWI547477B (zh) | 2012-03-14 | 2016-09-01 | 大賽璐股份有限公司 | 醋酸之製造方法 |
-
2008
- 2008-04-29 US US12/150,481 patent/US7820855B2/en active Active
-
2009
- 2009-04-08 TW TW098111613A patent/TW200946493A/zh unknown
- 2009-04-23 JP JP2011507417A patent/JP5507544B2/ja active Active
- 2009-04-23 KR KR1020107026617A patent/KR20110003555A/ko not_active Application Discontinuation
- 2009-04-23 WO PCT/US2009/002506 patent/WO2009134333A1/en active Application Filing
- 2009-04-23 NZ NZ588701A patent/NZ588701A/en not_active IP Right Cessation
- 2009-04-23 MX MX2014001618A patent/MX338852B/es unknown
- 2009-04-23 DE DE9739136T patent/DE09739136T1/de active Pending
- 2009-04-23 CN CN200980115410.8A patent/CN102015088B/zh active Active
- 2009-04-23 SG SG2013032586A patent/SG190600A1/en unknown
- 2009-04-23 AU AU2009241844A patent/AU2009241844A1/en not_active Abandoned
- 2009-04-23 EP EP09739136.1A patent/EP2323755B1/en active Active
- 2009-04-23 EP EP15002793.6A patent/EP3002057B1/en active Active
- 2009-04-23 ES ES15002793.6T patent/ES2694014T3/es active Active
- 2009-04-23 RU RU2010148399/05A patent/RU2508162C2/ru not_active IP Right Cessation
- 2009-04-23 CA CA2721922A patent/CA2721922C/en active Active
- 2009-04-23 MX MX2010011852A patent/MX2010011852A/es active IP Right Grant
- 2009-04-23 ES ES09739136.1T patent/ES2365906T3/es active Active
- 2009-04-23 MX MX2015017656A patent/MX364125B/es unknown
- 2009-04-23 BR BRPI0911487-4A patent/BRPI0911487B1/pt active IP Right Grant
- 2009-04-28 CL CL2009001003A patent/CL2009001003A1/es unknown
- 2009-04-29 AR ARP090101531A patent/AR074141A1/es not_active Application Discontinuation
-
2010
- 2010-09-23 US US12/924,234 patent/US8329944B2/en active Active
- 2010-10-20 ZA ZA2010/07491A patent/ZA201007491B/en unknown
-
2011
- 2011-03-22 ZA ZA2011/02114A patent/ZA201102114B/en unknown
- 2011-10-13 HK HK11110937.2A patent/HK1156560A1/xx not_active IP Right Cessation
-
2012
- 2012-11-05 US US13/668,577 patent/US8771616B2/en active Active
-
2014
- 2014-07-08 US US14/325,773 patent/US8987512B2/en active Active
-
2015
- 2015-03-09 US US14/642,327 patent/US9840451B2/en active Active
-
2017
- 2017-11-09 US US15/808,401 patent/US10118885B2/en active Active
-
2018
- 2018-10-25 US US16/170,781 patent/US10519089B2/en active Active
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CL2009001003A1 (es) | Proceso de carbonilacion para producir acido acetico que comprende carbonilar metanol, alimentar la mezcla de reaccion a un deposito de vaporizacion y calentar, donde la corriente de vapor del producto sin refinar conserva una temperatura superior a 148,88 grados celsius y la concentracion de acido acetico superior a 70% en peso. | |
AR075072A1 (es) | Proceso para formar etileno a partir de acido acetico de manera selectiva | |
CL2011001612A1 (es) | Proceso de produccion de acetato de vinilo que comprende: contactar una corriente de alimentacion de acido acetico e hidrogeno a temperatura elevada con catalizador de hidrogenacion, enriquecer la corriente con acetato de etilo,contactar la corriente con un catalizador de cracking, y separar el acetato de vinilo | |
NZ628248A (en) | Process for the acetylation of wood and acetylated wood | |
AR074712A1 (es) | Procesos para formar etanol directa y selectivamente a partir de acido acetico | |
WO2012167790A3 (en) | Process for producing liquid hydrocarbon | |
GB201213579D0 (en) | Desalination system and method for desalination | |
CL2008003206A1 (es) | Metodo para remover acetaldehido desde mezcla de acetato de metilo, metanol y ach que comprende: alimentar la mezcla a una columna de destilacion; destilar la mezcla a 10 psig o mas, y generar corriente de vapor enriquecida en ach, y retirar la corriente de residuos reducida en ach; proceso para producir acido acetico | |
UA96032C2 (en) | Process for the production of methyl acetate | |
CO6561810A2 (es) | Proceso para evaporar ácido acético para procesos de hidrogenación para producir etanol | |
BR112012019035A2 (pt) | "processo para vaporização de ácido acético para processos de hidrogenação para produzir etanol". | |
UA100016C2 (en) | Process for the production of methyl acetate | |
BRPI0908218A2 (pt) | processo para a produção de ácido acético | |
AR086053A1 (es) | Control de agua en la produccion de alcohol a partir de una hidrogenacion | |
TW200720243A (en) | Process for stably operating a continuous preparation process for obtaining acrolein or acrylic acid or a mixture thereof from propane | |
CN101990517B (zh) | 制备合成气的方法ii | |
RU2016146790A (ru) | Способ совместного получения уксусной кислоты и диметилового эфира | |
BR112012023045A2 (pt) | processo para produzir hidrogênio | |
BR112013011436A2 (pt) | processo para a coprodução de anidrido acético e de ácido acético | |
BRPI0716517A8 (pt) | Processos para a produção de uma mistura em fase vapor e para a produção de metanol | |
AR082709A1 (es) | Metodo de carbonilacion para producir acido acetico | |
JP2013537549A5 (es) | ||
RU2009145850A (ru) | Способ получения изопрена | |
AR072760A1 (es) | Procedimiento mejorado para preparar acido cianhidrico | |
WO2011110731A3 (en) | Method and apparatus for accelerating biotechnical reaction and production |