GB690977A - Improvements in or relating to oxo synthesis - Google Patents
Improvements in or relating to oxo synthesisInfo
- Publication number
- GB690977A GB690977A GB14516/51A GB1451651A GB690977A GB 690977 A GB690977 A GB 690977A GB 14516/51 A GB14516/51 A GB 14516/51A GB 1451651 A GB1451651 A GB 1451651A GB 690977 A GB690977 A GB 690977A
- Authority
- GB
- United Kingdom
- Prior art keywords
- cobalt
- aldehyde
- dissolved
- solvent
- acid
- 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C27/00—Processes involving the simultaneous production of more than one class of oxygen-containing compounds
- C07C27/20—Processes involving the simultaneous production of more than one class of oxygen-containing compounds by oxo-reaction
- C07C27/22—Processes involving the simultaneous production of more than one class of oxygen-containing compounds by oxo-reaction with the use of catalysts which are specific for this process
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Aldehydes containing dissolved cobalt compounds produced by the Oxo synthesis are treated in a catalyst removal zone with oxalic acid to precipitate cobalt oxalate. The acid may be added as a solid or dissolved in a non-aqueous solvent, e.g. ether, acetone, dioxane, or decobalted aldehyde product, if desired after dehydration. Generally a molar equivalent up to 10 per cent excess of acid is used at about 70-160 DEG F. After settling, the separated aldehyde may be filtered and water-washed, and the solvent, if used, separated by flash distillation. Removal of the solvent may, however, be effected after hydrogenation of the aldehyde to alcohol. Soluble or insoluble cobalt compounds may be added in starting up, e.g. cobalt naphthenate or oleate dissolved in the olefin feed or cobalt oxalate. Preferred conditions are 250-450 DEG F., and 2500-3500 p.s.i.g. Part of the reaction product containing dissolved cobalt, and of the suspension of precipitated cobalt oxalate prior to settling, may be recycled to the reactor.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US690977XA | 1951-03-29 | 1951-03-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB690977A true GB690977A (en) | 1953-04-29 |
Family
ID=22086745
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB14516/51A Expired GB690977A (en) | 1951-03-29 | 1951-06-19 | Improvements in or relating to oxo synthesis |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB690977A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4625067A (en) * | 1984-11-30 | 1986-11-25 | Exxon Research & Engineering Co. | Hydroformylation catalyst removal |
-
1951
- 1951-06-19 GB GB14516/51A patent/GB690977A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4625067A (en) * | 1984-11-30 | 1986-11-25 | Exxon Research & Engineering Co. | Hydroformylation catalyst removal |
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