HK33092A - Process for regenerating a carbonylation catalyst solution to remove corrosion metals - Google Patents
Process for regenerating a carbonylation catalyst solution to remove corrosion metals Download PDFInfo
- Publication number
- HK33092A HK33092A HK330/92A HK33092A HK33092A HK 33092 A HK33092 A HK 33092A HK 330/92 A HK330/92 A HK 330/92A HK 33092 A HK33092 A HK 33092A HK 33092 A HK33092 A HK 33092A
- Authority
- HK
- Hong Kong
- Prior art keywords
- acetic acid
- lithium
- catalyst
- catalyst solution
- carbonylation
- 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
- 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
-
- 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
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/04—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing carboxylic acids or their salts
-
- 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
- B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
- B01J31/08—Ion-exchange resins
-
- 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
- B01J31/40—Regeneration or reactivation
- B01J31/4015—Regeneration or reactivation of catalysts containing metals
- B01J31/4023—Regeneration or reactivation of catalysts containing metals containing iron group metals, noble metals or copper
- B01J31/4038—Regeneration or reactivation of catalysts containing metals containing iron group metals, noble metals or copper containing noble metals
- B01J31/4046—Regeneration or reactivation of catalysts containing metals containing iron group metals, noble metals or copper containing noble metals containing rhodium
-
- 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
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
- B01J2231/34—Other additions, e.g. Monsanto-type carbonylations, addition to 1,2-C=X or 1,2-C-X triplebonds, additions to 1,4-C=C-C=X or 1,4-C=-C-X triple bonds with X, e.g. O, S, NH/N
-
- 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
-
- 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
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Carbon And Carbon Compounds (AREA)
Claims (11)
- Procédé pour la régénération de solutions catalytiques de carbonylation contenant du rhodium et du lithium et contenant en outre des produits métalliques corrosifs de contamination, qui consiste à mettre en contact intime ladite solution catalytique avec une résine échangeuse de cations sous la forme lithium et à récupérer une solution catalytique de teneur réduite en produits métalliques de contamination.
- Procédé suivant la revendication 1, caractérisé en ce que la résine est une résine échangeuse de cations du type à acide fort.
- Procédé suivant la revendication 1 ou 2, caractérisé en ce que la mise en contact est effectuée en faisant passer la solution catalytique au travers d'une colonne à lit fixe de la résine.
- Procédé suivant l'une des revendications 1 à 3, caractérisé en ce que la résine est régénérée après épuisement par lavage avec un sel de lithium.
- Procédé suivant la revendication 4, caractérisé en ce que le sel de lithium est dissous dans une solution de régénération d'eau et d'acide acétique.
- Procédé suivant la revendication 5, caractérisé en ce que l'acide acétique constitue de 0,1 à 95% en poids de la solution de régénération.
- Procédé suivant la revendication 6, caractérisé en ce que l'acide acétique constitue de 0,1 à 20% en poids de la solution de régénération.
- Procédé suivant l'une des revendications 5 à 7, caractérisé en ce que le sel de lithium est présent suivant une quantité comprise entre 1 et 20% en poids.
- Procédé suivant l'une des revendications 4 à 8, caractérisé en ce que le sel de lithium est de l'acétate de lithium.
- Procédé suivant l'une des revendications 1 à 9, caractérisé en ce que les produits métalliques corrosifs de contamination comprennent le fer, le nickel, le chrome ou le molybdène ou un mélange quelconque de ceux-ci.
- Procédé suivant l'une des revendications 1 à 10, caractérisé en ce que la solution catalytique de carbonylation est d'abord obtenue comme un flux de procédé à partir d'un procédé pour la carbonylation du méthanol pour le transformer en acide acétique dans un réacteur de carbonylation en faisant passer du monoxyde de carbone dans un milieu réactionnel contenu dans le réacteur et comprenant du méthanol et une solution catalytique de faible teneur en eau comprenant du rhodium, un agent initiateur d'iodure de méthyle, de l'acétate de méthyle et de l'iodure de lithium pour produire de l'acide acétique et ledit acide acétique est récupérée à partir de l'effluent du réacteur en concentrant l'effluent en une variété de flux de procédé comprenant un ou plusieurs des composés de la solution catalytique et du produit d'acide acétique.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/918,740 US4894477A (en) | 1986-10-14 | 1986-10-14 | Process for regenerating a carbonylation catalyst solution to remove corrosion metals and carbonylation of methanol to acetic acid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| HK33092A true HK33092A (en) | 1992-05-15 |
Family
ID=25440880
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| HK330/92A HK33092A (en) | 1986-10-14 | 1992-05-07 | Process for regenerating a carbonylation catalyst solution to remove corrosion metals |
Country Status (15)
| Country | Link |
|---|---|
| US (1) | US4894477A (fr) |
| EP (1) | EP0265140B1 (fr) |
| JP (1) | JPH0811199B2 (fr) |
| CN (2) | CN1017314B (fr) |
| AT (1) | ATE69176T1 (fr) |
| AU (1) | AU620020B2 (fr) |
| BR (1) | BR8705501A (fr) |
| CA (1) | CA1306237C (fr) |
| DD (1) | DD266282A5 (fr) |
| DE (1) | DE3774393D1 (fr) |
| ES (1) | ES2027299T3 (fr) |
| GR (1) | GR3003078T3 (fr) |
| HK (1) | HK33092A (fr) |
| MX (1) | MX165480B (fr) |
| SG (1) | SG20392G (fr) |
Families Citing this family (41)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5155265A (en) * | 1987-12-23 | 1992-10-13 | Hoechst Celanese Corporation | Purification of acetic acid with ozone followed by treatment with activated carbon and/or an ion-exchange resin |
| US5202481A (en) * | 1987-12-23 | 1993-04-13 | Hoechst Celanese Corporation | Purification of acetic acid produced by the low water carbonylation of methanol by treatment with ozone |
| DE3823645C1 (fr) * | 1988-07-13 | 1989-11-30 | Hoechst Ag | |
| DE3903909A1 (de) * | 1989-02-10 | 1990-08-16 | Hoechst Ag | Verfahren zur entfernung metallischer korrosionsprodukte aus einer bei der carbonylierung von methanol und/oder methylacetat und/oder dimethylether anfallenden, verunreinigten katalysatorloesung |
| GB8904125D0 (en) † | 1989-02-23 | 1989-04-05 | British Petroleum Co Plc | Process for preparing carboxylic acids |
| US5218143A (en) * | 1989-02-23 | 1993-06-08 | The British Petroleum Company P.L.C. | Process for preparing carboxylic acids |
| DE4034501A1 (de) * | 1990-10-30 | 1992-05-07 | Hoechst Ag | Verfahren zur entfernung metallischer korrosionsprodukte aus wasserfrei betriebenen carbonylierungsreaktionen |
| GB9122168D0 (en) * | 1991-10-18 | 1991-11-27 | Bp Chem Int Ltd | Process |
| GB9211671D0 (en) * | 1992-06-02 | 1992-07-15 | Bp Chem Int Ltd | Process |
| GB9305902D0 (en) * | 1993-03-22 | 1993-05-12 | Bp Chem Int Ltd | Process |
| CN1043013C (zh) * | 1993-06-24 | 1999-04-21 | 黑龙江省科学院石油化学研究所 | 醋酸溶液中钴锰离子的离子交换回收方法 |
| US5352415A (en) * | 1993-09-29 | 1994-10-04 | Hoechst Celanese Corporation | Control system for acetic acid manufacturing process |
| US5625095A (en) * | 1994-06-15 | 1997-04-29 | Daicel Chemical Industries, Ltd. | Process for producing high purity acetic acid |
| CA2234853C (fr) * | 1995-10-27 | 2005-01-11 | Hoechst Celanese Corporation | Procede pour ameliorer la productivite d'une solution de catalyseur de carbonylation, par l'elimination des metaux de corrosion |
| SG65716A1 (en) * | 1996-12-30 | 1999-06-22 | Chiyoda Chem Eng Construct Co | Process for the production of carbonyl compound |
| GB0410289D0 (en) * | 2004-05-07 | 2004-06-09 | Bp Chem Int Ltd | Process |
| JP4657632B2 (ja) * | 2004-05-27 | 2011-03-23 | ダイセル化学工業株式会社 | カルボン酸の製造方法 |
| CN1309324C (zh) * | 2005-05-16 | 2007-04-11 | 索连江 | 保健食品香烟及其制备方法 |
| US8785684B2 (en) | 2010-06-14 | 2014-07-22 | Celanese International Corporation | Methanol carbonylation process with rhodium catalyst, an iodide salt and a metallic co-catalyst selected from transition metals, indium, strontium, barium, zinc, tin and heteropoly acids |
| US8835681B2 (en) | 2010-06-14 | 2014-09-16 | Celanese International Corporation | Methanol carbonylation process with rhodium catalyst and a lanthanide metal co-catalyst |
| WO2011159268A1 (fr) | 2010-06-14 | 2011-12-22 | Celanese Internaltional Corporation | Procédé de carbonylation |
| US8378141B2 (en) | 2010-08-16 | 2013-02-19 | Celanese International Corporation | Process and system for supplying vapor from drying column to light ends column |
| US8461379B2 (en) | 2010-10-12 | 2013-06-11 | Celanese International Corporation | Production of acetic acid comprising feeding at least one reactant to a recycle stream |
| BR112013009012A2 (pt) | 2010-10-13 | 2016-07-12 | Celanese Int Corp | processo para a recuperação de promotores de halogêneo e romoção de compostos redutores de permanganato |
| US8637698B2 (en) | 2010-11-19 | 2014-01-28 | Celanese International Corporation | Production of acetic acid with an increased production rate |
| CN103370300B (zh) | 2010-12-15 | 2016-07-06 | 株式会社大赛璐 | 乙酸的制备方法 |
| US8697908B2 (en) * | 2011-05-05 | 2014-04-15 | Celanese International Corporation | Removal of amine compounds from carbonylation process stream containing corrosion metal contaminants |
| US8952196B2 (en) | 2011-05-05 | 2015-02-10 | Celanese International Corporation | Removal of aromatics from carbonylation process |
| TWI547477B (zh) | 2012-03-14 | 2016-09-01 | 大賽璐股份有限公司 | 醋酸之製造方法 |
| US8859810B2 (en) | 2012-08-21 | 2014-10-14 | Celanese International Corporation | Process for recovering permanganate reducing compounds from an acetic acid production process |
| CN115636745A (zh) * | 2014-11-14 | 2023-01-24 | 国际人造丝公司 | 通过去除铁改进乙酸产率的方法 |
| US9540302B2 (en) | 2015-04-01 | 2017-01-10 | Celanese International Corporation | Processes for producing acetic acid |
| US9540303B2 (en) | 2015-04-01 | 2017-01-10 | Celanese International Corporation | Processes for producing acetic acid |
| US9822055B2 (en) * | 2015-06-23 | 2017-11-21 | Lyondellbasell Acetyls, Llc | Silver loaded halide removal resins for treating halide containing solutions |
| US9957216B2 (en) | 2015-11-13 | 2018-05-01 | Celanese International Corporation | Processes for producing acetic acid |
| JP6786308B2 (ja) * | 2016-08-30 | 2020-11-18 | 月島環境エンジニアリング株式会社 | 陽イオン交換樹脂の再生方法、被処理液の処理方法及び陽イオン交換樹脂を含む処理設備 |
| CN109467499B (zh) * | 2018-08-03 | 2025-01-10 | 天津大学 | 聚乙烯醇母液回收过程中醋酸甲酯水解与醋酸精制的防腐工艺及装置 |
| CN110124755B (zh) * | 2019-06-06 | 2021-12-17 | 上海华谊(集团)公司 | 链烷酸的制造方法 |
| CN110078612B (zh) * | 2019-06-06 | 2021-09-07 | 上海华谊(集团)公司 | 催化剂循环液的纯化方法 |
| JP7641198B2 (ja) * | 2021-07-14 | 2025-03-06 | オルガノ株式会社 | リチウム水溶液の精製方法 |
| CN116159488B (zh) * | 2022-12-30 | 2025-09-30 | 上海浦景化工新材料有限公司 | 一种甲醇低压羰基化制备醋酸的系统及方法 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4007130A (en) * | 1975-12-29 | 1977-02-08 | Monsanto Company | Catalyst regeneration method |
| DE2614799C2 (de) * | 1976-04-06 | 1986-02-27 | Basf Ag, 6700 Ludwigshafen | Verfahren zur Regenerierung von Rhodium enthaltenden Katalysatoren durch Behandeln von rhodiumhaltigen Destillationsrückständen von Hydroformylierungsgemischen |
| DE2950318C2 (de) * | 1979-12-14 | 1982-02-25 | Dynamit Nobel Ag, 5210 Troisdorf | Gewinnung und Wiederverwendung von Kobalt- oder Kobalt und Manganverbindungen aus dem Witten-DMT-Prozeß |
| US4388217A (en) * | 1980-11-24 | 1983-06-14 | Eastman Kodak Company | Process for the recovery of catalyst values |
| CA1228867A (fr) * | 1984-05-03 | 1987-11-03 | Celanese Corporation | Carbonylation du methanol |
-
1986
- 1986-10-14 US US06/918,740 patent/US4894477A/en not_active Expired - Lifetime
-
1987
- 1987-10-02 AU AU79319/87A patent/AU620020B2/en not_active Expired
- 1987-10-05 CA CA000548577A patent/CA1306237C/fr not_active Expired - Lifetime
- 1987-10-13 EP EP87309013A patent/EP0265140B1/fr not_active Expired - Lifetime
- 1987-10-13 AT AT87309013T patent/ATE69176T1/de not_active IP Right Cessation
- 1987-10-13 DE DE8787309013T patent/DE3774393D1/de not_active Expired - Lifetime
- 1987-10-13 ES ES198787309013T patent/ES2027299T3/es not_active Expired - Lifetime
- 1987-10-13 MX MX008816A patent/MX165480B/es unknown
- 1987-10-14 BR BR8705501A patent/BR8705501A/pt not_active IP Right Cessation
- 1987-10-14 DD DD87307941A patent/DD266282A5/de not_active IP Right Cessation
- 1987-10-14 JP JP62257478A patent/JPH0811199B2/ja not_active Expired - Fee Related
- 1987-10-14 CN CN87106904A patent/CN1017314B/zh not_active Expired
-
1991
- 1991-11-07 GR GR91401687T patent/GR3003078T3/el unknown
-
1992
- 1992-02-11 CN CN92100807A patent/CN1029841C/zh not_active Expired - Lifetime
- 1992-02-29 SG SG203/92A patent/SG20392G/en unknown
- 1992-05-07 HK HK330/92A patent/HK33092A/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| EP0265140A1 (fr) | 1988-04-27 |
| DD266282A5 (de) | 1989-03-29 |
| BR8705501A (pt) | 1988-05-24 |
| ES2027299T3 (es) | 1992-06-01 |
| CN87106904A (zh) | 1988-07-20 |
| US4894477A (en) | 1990-01-16 |
| ATE69176T1 (de) | 1991-11-15 |
| CA1306237C (fr) | 1992-08-11 |
| AU620020B2 (en) | 1992-02-13 |
| DE3774393D1 (de) | 1991-12-12 |
| SG20392G (en) | 1992-04-16 |
| MX165480B (es) | 1992-11-13 |
| AU7931987A (en) | 1988-04-21 |
| GR3003078T3 (en) | 1993-02-17 |
| CN1029841C (zh) | 1995-09-27 |
| JPH0811199B2 (ja) | 1996-02-07 |
| EP0265140B1 (fr) | 1991-11-06 |
| CN1062721A (zh) | 1992-07-15 |
| JPS63116746A (ja) | 1988-05-21 |
| CN1017314B (zh) | 1992-07-08 |
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| EP0618185B1 (fr) | Procédé de séparation de métaux corrosifs contaminant à partir de compositions liquides | |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PF | Patent in force | ||
| PE | Patent expired |
Effective date: 20071012 |