GB909941A - Condensation of ketones to prepare higher molecular weight ketones - Google Patents
Condensation of ketones to prepare higher molecular weight ketonesInfo
- Publication number
- GB909941A GB909941A GB2425660A GB2425660A GB909941A GB 909941 A GB909941 A GB 909941A GB 2425660 A GB2425660 A GB 2425660A GB 2425660 A GB2425660 A GB 2425660A GB 909941 A GB909941 A GB 909941A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ketones
- oxide
- ketone
- group
- catalyst
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/06—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of zinc, cadmium or mercury
-
- 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
- C07C45/74—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 dehydration
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
Catalysts suitable for converting C3-C6 ketones to higher ketones comprise 70-84% (by weight) of a Group II(a) metal oxide (Zn, Cd or Hg) and 16-30% of a Group IV (a) metal oxide (Ti, Zr or Hf). The catalyst is preferably supported on an inert carrier such as brass turning, metallic chips, pumice, porcelain, g -alumina or calcined coke. The preferred catalysts are those containing 80-84% of zinc oxide and 16-20% of zirconium oxide.ALSO:Higher molecular weight ketones are made by contacting at an elevated temperature an acyclic C3-C6 ketone with a catalyst comprising 70-84% (by weight) of a Group IIb metal oxide and 16-30% of a Group IVa (titanium sub-group) metal oxide. The catalyst is preferably supported, for example on brass turnings, metallic chips, pumice, porcelain, g -alumina or calcined coke. The preferred temperature range for carrying out the process is 780-850 DEG F. and the preferred pressures are from atmospheric to 5 atmospheres. An improved yield is obtained if hydrogen is introduced into the reaction mixture. The preferred catalyst is one containing 80-84% of zinc oxide and 16-20% of zirconium oxide. Suitable starting ketones are, for example, methylethyl ketone, methylpropyl ketone and methylisopropyl ketone. In the examples acetone is converted to mesityl oxide with some methyl isobutyl ketone, higher ketones, phorone and isophorone. The mesityl oxide may be catalytically hydrogenated to give methyl isobutyl ketone.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US84002259A | 1959-09-15 | 1959-09-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB909941A true GB909941A (en) | 1962-11-07 |
Family
ID=25281260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2425660A Expired GB909941A (en) | 1959-09-15 | 1960-07-12 | Condensation of ketones to prepare higher molecular weight ketones |
Country Status (3)
Country | Link |
---|---|
BE (1) | BE595084A (en) |
DE (1) | DE1210805B (en) |
GB (1) | GB909941A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1232942B (en) * | 1963-10-30 | 1967-01-26 | Distillers Co Yeast Ltd | Process for the production of higher ketones |
FR2156246A1 (en) * | 1971-10-13 | 1973-05-25 | Basf Ag | |
US4535187A (en) * | 1983-12-21 | 1985-08-13 | Union Carbide Corporation | Preparation of isophorone and mesityl oxide from acetone |
EP1103538A1 (en) * | 1999-11-24 | 2001-05-30 | Oxeno Olefinchemie GmbH | Process for carrying out aldolcondensations |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE908018C (en) * | 1942-04-26 | 1954-04-01 | Dortmunder Paraffinwerke Ges M | Process for the catalytic conversion of acetone |
-
1960
- 1960-07-12 GB GB2425660A patent/GB909941A/en not_active Expired
- 1960-08-23 DE DEE19814A patent/DE1210805B/en active Pending
- 1960-09-15 BE BE595084A patent/BE595084A/en unknown
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1232942B (en) * | 1963-10-30 | 1967-01-26 | Distillers Co Yeast Ltd | Process for the production of higher ketones |
FR2156246A1 (en) * | 1971-10-13 | 1973-05-25 | Basf Ag | |
US4535187A (en) * | 1983-12-21 | 1985-08-13 | Union Carbide Corporation | Preparation of isophorone and mesityl oxide from acetone |
EP1103538A1 (en) * | 1999-11-24 | 2001-05-30 | Oxeno Olefinchemie GmbH | Process for carrying out aldolcondensations |
SG90201A1 (en) * | 1999-11-24 | 2002-07-23 | Oxeno Olefinchemie Gmbh | Process for carrying out aldol condensations |
KR100622288B1 (en) * | 1999-11-24 | 2006-09-11 | 옥세노 올레핀케미 게엠베하 | Process for carrying out aldol condensations |
Also Published As
Publication number | Publication date |
---|---|
BE595084A (en) | 1961-03-15 |
DE1210805B (en) | 1966-02-17 |
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