GB1227977A - - Google Patents
Info
- Publication number
- GB1227977A GB1227977A GB1227977DA GB1227977A GB 1227977 A GB1227977 A GB 1227977A GB 1227977D A GB1227977D A GB 1227977DA GB 1227977 A GB1227977 A GB 1227977A
- Authority
- GB
- United Kingdom
- Prior art keywords
- metal
- hydrogen
- resin
- ion exchanger
- palladium
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
- B01J31/28—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of the platinum group metals, iron group metals or copper
-
- 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
- B01J31/02—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
- B01J31/10—Ion-exchange resins sulfonated
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
- C07C45/67—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
- C07C45/68—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
- C07C45/72—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms by reaction of compounds containing >C = O groups with the same or other compounds containing >C = O groups
- C07C45/73—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms by reaction of compounds containing >C = O groups with the same or other compounds containing >C = O groups combined with hydrogenation
-
- 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
- B01J2231/349—1,2- or 1,4-additions in combination with further or prior reactions by the same catalyst, i.e. tandem or domino reactions, e.g. hydrogenation or further addition reactions
Abstract
1,227,977. Noble metal catalysts. SCHOLVEN-CHEMIE A.G. 26 Aug., 1968 [8 Sept., 1967], No. 40751/68. Heading B1E. [Also in Division C2] A catalyst for the reaction of acetone with hydrogen to produce methyl isobutyl ketone is prepared by a partial ion exchange reaction in aqueous solution of the H ions of a strongly acid ion exchanger for the metal cations of a salt of a noble metal of Group VIII of the Periodic Table, with subsequent washing and reduction with hydrogen to convert the metal cations into metallic atoms. The metal is preferably palladium and the ion exchanger may be a macroporous sulphonated polystyron/divinylbenzol resin. The catalyst is prepared by treating an aqueous solution of the metal salt (e.g. palladium nitrate) with the acidic ion exchanger when the metal ions are quantitatively taken up. The resin is then washed with water and treated with hydrogen to restore the resin to the H+ form having the metal distributed largely in monomolecular form throughout its structure. The final catalyst preferably contains 0.001-0.5% by weight of palladium.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19671643044 DE1643044C3 (en) | 1967-09-08 | 1967-09-08 | Process for the production of methyl isobutyl ketone |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1227977A true GB1227977A (en) | 1971-04-15 |
Family
ID=5684243
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1227977D Expired GB1227977A (en) | 1967-09-08 | 1968-08-26 |
Country Status (3)
Country | Link |
---|---|
CH (1) | CH526494A (en) |
FR (1) | FR1579809A (en) |
GB (1) | GB1227977A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0251167A2 (en) * | 1986-06-25 | 1988-01-07 | Union Carbide Corporation | Process for the condensation of ketones |
EP1184076A1 (en) * | 1999-11-17 | 2002-03-06 | Japan Science and Technology Corporation | Polymer-supported lewis acid catalyst |
EP1321450A2 (en) * | 2001-12-19 | 2003-06-25 | Rohm And Haas Company | Metal-doped sulfonated ion exchange resin catalysts |
EP2532642A3 (en) * | 2011-06-07 | 2013-11-13 | King Abdulaziz City for Science & Technology (KACST) | Low pressure one-step gas-phase process for production of methyl isobutyl ketone |
CN116041158A (en) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | Method for preparing methyl isobutyl ketone by liquid phase hydrogenation of 4-methyl-3-pentene-2-one |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1085879B (en) | 1976-04-08 | 1985-05-28 | Basf Ag | PROCESS FOR THE PREPARATION OF SUPERIOR KETONES |
-
1968
- 1968-08-26 CH CH1278668A patent/CH526494A/en not_active IP Right Cessation
- 1968-08-26 GB GB1227977D patent/GB1227977A/en not_active Expired
- 1968-09-09 FR FR1579809D patent/FR1579809A/fr not_active Expired
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0251167A2 (en) * | 1986-06-25 | 1988-01-07 | Union Carbide Corporation | Process for the condensation of ketones |
EP0251167A3 (en) * | 1986-06-25 | 1990-01-31 | Union Carbide Corporation | Process for the condensation of ketones |
EP1184076A1 (en) * | 1999-11-17 | 2002-03-06 | Japan Science and Technology Corporation | Polymer-supported lewis acid catalyst |
EP1184076A4 (en) * | 1999-11-17 | 2005-04-13 | Japan Science & Tech Agency | Polymer-supported lewis acid catalyst |
EP1321450A2 (en) * | 2001-12-19 | 2003-06-25 | Rohm And Haas Company | Metal-doped sulfonated ion exchange resin catalysts |
EP1321450A3 (en) * | 2001-12-19 | 2003-09-03 | Rohm And Haas Company | Metal-doped sulfonated ion exchange resin catalysts |
CN1325458C (en) * | 2001-12-19 | 2007-07-11 | 罗姆和哈斯公司 | Metal doped sulfunated ion exchange resin catalyst |
KR100940327B1 (en) * | 2001-12-19 | 2010-02-04 | 롬 앤드 하스 캄파니 | Metal-Doped Sulfonated Ion Exchange Resin Catalysts |
EP2532642A3 (en) * | 2011-06-07 | 2013-11-13 | King Abdulaziz City for Science & Technology (KACST) | Low pressure one-step gas-phase process for production of methyl isobutyl ketone |
CN116041158A (en) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | Method for preparing methyl isobutyl ketone by liquid phase hydrogenation of 4-methyl-3-pentene-2-one |
Also Published As
Publication number | Publication date |
---|---|
CH526494A (en) | 1972-08-15 |
FR1579809A (en) | 1969-08-29 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |