SE300815B - - Google Patents
Info
- Publication number
- SE300815B SE300815B SE1243162A SE1243162A SE300815B SE 300815 B SE300815 B SE 300815B SE 1243162 A SE1243162 A SE 1243162A SE 1243162 A SE1243162 A SE 1243162A SE 300815 B SE300815 B SE 300815B
- Authority
- SE
- Sweden
- Prior art keywords
- elevated temperature
- calcining
- zinc oxide
- drying
- hours
- Prior art date
Links
Classifications
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- 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
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- 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
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/28—Molybdenum
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- 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
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/34—Manganese
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C49/00—Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
- C07C49/20—Unsaturated compounds containing keto groups bound to acyclic carbon atoms
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
Alpha, beta-unsaturated carbonyl compounds are prepared by contacting a liquid feed containg a monofunctional, aliphatic C2 to C20 aldehyde and/or ketone having at least two alpha hydrogen atoms at from 50 DEG to 600 DEG C. with a catalyst produced by reacting together at elevated temperature the trioxide of molybdenum and an oxide of magnesium or other compounds of these metals which produce these oxides at the elevated temperature. The catalyst may be utilized alone or in combination with a support or carrier, e.g. alumina, and, in a modified process, may also contain zinc oxide. In a further modification, the feed also comprises a monofunctional, aliphatic aldehyde or ketone, e.g. formaldehyde.ALSO:An amorphous spinel-type material is obtained by reacting together at an elevated temperature, generally 300 DEG to 1500 DEG F., the trioxide of molybdenium and an oxide of magnesium or other compounds of these metals which produce these oxides at the elevated temperature. If zinc oxide or a compound which produces zinc oxide at the elevated temperature is present the zinc oxide is physically entrapped in the spinel product formed. In an example, a spinel-type product is obtained by dry-mixing equimolar amounts of ammonium molybdate and magnesium oxide in powder form, adding water to form a paste, drying said paste at 400 DEG F. for 16 hours, pilling the crushed and ground product and finally calcining the pills at 1100 DEG F. for 16 hours. Similar processes for the preparation of zinc oxide containing products are also described.ALSO:A catalyst is prepared by reacting together at an elevated temperature, generally 300-1500 DEG F., the trioxide of molybdenum, an oxide of magnesium and zinc oxide or other compounds of these metals which produce these oxides at the elevated temperature. The catalyst may be utilized above or in combination with a support or carrier, especially alumina. In the examples, the catalyst is produced by (A) dry-mixing equimolar amounts of MoO3, MgO and ZnO in powder form, adding water to form a paste, drying said paste at 300 DEG F., pilling the crushed and ground product and calcining the pills at 1100 DEG F. for 16 hours, and (B) calcining alumina at 1000 DEG F. for 16 hours, impregnating the alumina with ammonium molybdate solution, drying the impregnated alumina at 250 DEG F. prior to calcining at 1000 DEG F. for 16 hours, impregnating the calcined product with magnesium nitrate solution, drying at 250 DEG F. prior to calcining at 850 DEG F. overnight, impregnating this calcined product with zinc nitrate solution, drying at 250 DEG F. and finally calcining the impregnated material at 850 DEG F. overnight.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US16163061A | 1961-12-22 | 1961-12-22 | |
| US161723A US3248428A (en) | 1961-12-22 | 1961-12-22 | Aldolization process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SE300815B true SE300815B (en) | 1968-05-13 |
Family
ID=26857983
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SE1243162A SE300815B (en) | 1961-12-22 | 1962-11-20 |
Country Status (3)
| Country | Link |
|---|---|
| DE (1) | DE1203243B (en) |
| GB (1) | GB1010695A (en) |
| SE (1) | SE300815B (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3542878A (en) * | 1967-11-22 | 1970-11-24 | Gulf Research Development Co | Aldol condensation process |
| BE789849A (en) * | 1971-10-13 | 1973-04-09 | Basf Ag | PROCESS FOR THE PREPARATION OF ALPHA-ETHYLENIC KETONES |
| US4169109A (en) | 1978-08-10 | 1979-09-25 | International Flavors & Fragrances Inc. | Process for preparing ketones using zinc acetate condensation catalysts, products produced thereby and organoleptic uses of same |
| US4535187A (en) * | 1983-12-21 | 1985-08-13 | Union Carbide Corporation | Preparation of isophorone and mesityl oxide from acetone |
| DE4020838A1 (en) * | 1990-06-29 | 1992-01-02 | Henkel Kgaa | Aldol condensn. of active hydrogen cpds. esp. fatty aldehyde - in presence of hydrated double layer hydroxide catalyst under azeotropic conditions, giving intermediates for surfactants and lubricants |
| GB9207756D0 (en) * | 1992-04-07 | 1992-05-27 | Davy Mckee London | Process |
| US6960694B2 (en) | 2003-07-01 | 2005-11-01 | Eastman Chemical Company | Processes for preparing β-hydroxy-ketones and α,β-unsaturated ketones |
| US7071361B2 (en) | 2004-06-25 | 2006-07-04 | Fastman Chemical Company | Processes for the preparation of high molecular weight saturated ketones |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE836346C (en) * | 1950-05-20 | 1952-04-10 | Ruhrchemie Ag | Process for the production of substituted acroleins |
| DE1051838B (en) * | 1951-04-25 | 1959-03-05 | Melle Usines Sa | Process for the production of unsaturated, higher molecular weight aliphatic aldehydes |
| US2852563A (en) * | 1955-10-17 | 1958-09-16 | Eastman Kodak Co | Condensation of isoaldehydes with lower aliphatic aldehydes |
| DE1084711B (en) * | 1956-05-07 | 1960-07-07 | Armour & Co | Process for the preparation of high molecular weight ª,ª-unsaturated aldehydes |
| US2921089A (en) * | 1957-11-27 | 1960-01-12 | Eastman Kodak Co | 2-propylheptanol and its esters |
| FR1224715A (en) * | 1958-05-27 | 1960-06-27 | Eastman Kodak Co | Process for the preparation of unsaturated aliphatic aldehydes |
-
1962
- 1962-11-07 GB GB4209762A patent/GB1010695A/en not_active Expired
- 1962-11-20 SE SE1243162A patent/SE300815B/xx unknown
- 1962-12-19 DE DEE24050A patent/DE1203243B/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| GB1010695A (en) | 1965-11-24 |
| DE1203243B (en) | 1965-10-21 |
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