GB342670A - Improvements in the refining of fatty acids obtained by the oxidation of paraffin wax or other high molecular organic compounds - Google Patents
Improvements in the refining of fatty acids obtained by the oxidation of paraffin wax or other high molecular organic compoundsInfo
- Publication number
- GB342670A GB342670A GB3219029A GB3219029A GB342670A GB 342670 A GB342670 A GB 342670A GB 3219029 A GB3219029 A GB 3219029A GB 3219029 A GB3219029 A GB 3219029A GB 342670 A GB342670 A GB 342670A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fatty acids
- oxidation
- hydrogen
- acid
- reduced
- 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
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The crude fatty acids formed by the oxidation of paraffin wax or other high molecular organic compound with the higher oxides of nitrogen or nitric acid, are purified by heating or distillation below about 300 DEG C. with a reducing gas and, if desired, at increased pressure. Carbon monoxide, hydrogen or mixtures of these e.g. water or power gas may be used alone, or mixed with ammonia, steam or carbon dioxide as diluents. A hydrogenating catalyst may be used. The treatment may be effected in a tower filled with Raschig rings or clay, or in an autoclave. The nitrogen-containing fatty acids, formed during oxidation, are stated to be reduced or split off. The crude acids obtained by the oxidation of paraffin wax with nitrogen oxides after washing free from mineral acid, are then (1) distilled at 280 DEG C. in a current of hydrogen, or (2) reduced by zinc and dilute sulphuric acid at 60 DEG C., or (3) dispersed in an acid or alkaline electrolyte and reduced electrolytically, or (4) freed from unoxidized wax by warming with methyl alcohol, and treating the resulting alcoholic solution of fatty acids at 40 DEG C. with hydrogen in the presence of hydrochloric acid and platinum asbestos as catalysts. The solution may thereafter be further purified by treatment with chlorine water, hydrogen peroxide or distillation. The remaining traces of amido acids may be removed by petroleum ether. Specification 324,492, [Class 2 (iii), Dyes &c.], is referred to.ALSO:The crude fatty acids formed by the oxidation of paraffin wax or other high molecular organic compound with the higher oxides of nitrogen or nitric acid, are purified by heating or distilling below about 300 DEG C. with a reducing gas and, if desired, at increased pressure. Carbon monoxide, hydrogen or mixtures of these, e.g. power or water gas may be used, or mixed with ammonia, steam or carbon dioxide as diluents. A hydrogenating catalyst may be used. The treatment may be effected in a tower packed with Raschig rings or clay, or in an autoclave. The nitrogen-containing fatty acids formed during oxidation, are stated to be reduced or split off. The crude acids obtained by the oxidation of paraffin wax with nitrogen oxides after washing free from mineral acid, are then (1) distilled at 280 DEG C. in a current of hydrogen, or (2) reduced by zinc and dilute sulphuric acid at 60 DEG C., or (3) dispersed in an acid or alkaline electrolyte and reduced electrolytically, or (4) freed from unoxidized wax by warming with methyl alcohol, and treating the resulting alcoholic solution of fatty acids at 40 DEG C. with hydrogen in the presence of hydrochloric acid and platinum asbestos as a catalyst. The solution may thereafter be further purified by treatment with chlorine water, hydrogen peroxide or distillation. The remaining traces of amido-acids may be removed by petroleum ether. Specification 324,492, [Class 2 (iii), Dyes &c.], is referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3219029A GB342670A (en) | 1929-10-23 | 1929-10-23 | Improvements in the refining of fatty acids obtained by the oxidation of paraffin wax or other high molecular organic compounds |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3219029A GB342670A (en) | 1929-10-23 | 1929-10-23 | Improvements in the refining of fatty acids obtained by the oxidation of paraffin wax or other high molecular organic compounds |
Publications (1)
Publication Number | Publication Date |
---|---|
GB342670A true GB342670A (en) | 1931-01-23 |
Family
ID=10334680
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3219029A Expired GB342670A (en) | 1929-10-23 | 1929-10-23 | Improvements in the refining of fatty acids obtained by the oxidation of paraffin wax or other high molecular organic compounds |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB342670A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2485982A (en) * | 1944-03-13 | 1949-10-25 | Commercial Solvents Corp | Electrolytic production of aminoalcohols |
DE1009174B (en) * | 1952-11-19 | 1957-05-29 | Richfield Oil Corp | Process for the purification of toluic acids |
DE1017611B (en) * | 1953-12-31 | 1957-10-17 | Basf Ag | Process for the separation of accompanying substances from solid, crystalline substances or substance mixtures |
US6168388B1 (en) | 1999-01-21 | 2001-01-02 | Camco International, Inc. | Dual pump system in which the discharge of a first pump is used to power a second pump |
-
1929
- 1929-10-23 GB GB3219029A patent/GB342670A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2485982A (en) * | 1944-03-13 | 1949-10-25 | Commercial Solvents Corp | Electrolytic production of aminoalcohols |
DE1009174B (en) * | 1952-11-19 | 1957-05-29 | Richfield Oil Corp | Process for the purification of toluic acids |
DE1017611B (en) * | 1953-12-31 | 1957-10-17 | Basf Ag | Process for the separation of accompanying substances from solid, crystalline substances or substance mixtures |
US6168388B1 (en) | 1999-01-21 | 2001-01-02 | Camco International, Inc. | Dual pump system in which the discharge of a first pump is used to power a second pump |
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