GB714385A - Purification of acrylonitrile - Google Patents
Purification of acrylonitrileInfo
- Publication number
- GB714385A GB714385A GB18199/52A GB1819952A GB714385A GB 714385 A GB714385 A GB 714385A GB 18199/52 A GB18199/52 A GB 18199/52A GB 1819952 A GB1819952 A GB 1819952A GB 714385 A GB714385 A GB 714385A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hydrogen cyanide
- per cent
- acrylonitrile
- solid
- carbonate
- 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
- C07C253/00—Preparation of carboxylic acid nitriles
- C07C253/32—Separation; Purification; Stabilisation; Use of additives
- C07C253/34—Separation; Purification
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Monomeric acrylonitrile containing as impurities minor amounts of hydrogen cyanide as such or as lactonitrile is purified by treating with from 0.0001-0.5 per cent by weight of an alkali metal or alkaline earth metal oxide, hydroxide, carbonate or cyanide in solution or in solid form. The treatment may be effected with aqueous base, finely divided solid base or slurried or dispersed solid base in a non-reactive solvent for acrylonitrile such as a hydrocarbon at from room temperature up to the boiling point of the acrylonitrile. The hydrogen cyanide is converted into a material which is either precipitated or is absorbed on the basic material when the latter is used in solid form. The basic material is subsequently removed with the impurities by subjecting the treated mixture to distillation, filtration, decantation or centrifugation. In typical examples, a crude acrylonitrile containing 700 p.p.m. hydrogen cyanide and obtained by reacting acetylene with hydrogen cyanide and distilling the resulting product is agitated with (1) 0.125 per cent solid sodium hydroxide pellets and then filtered; (5) with 0.01 per cent sodium carbonate in water and the aqueous layer then removed; (6) with 0.001 per cent calcium hydroxide slurried in kerosene; or (7) 0.01 magnesium carbonate in benzene and the solvent layer then removed; in each case the hydrogen cyanide content is reduced to below 5 p.p.m. The use of the basic potassium compounds is also mentioned.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US714385XA | 1951-07-20 | 1951-07-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB714385A true GB714385A (en) | 1954-08-25 |
Family
ID=22101321
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB18199/52A Expired GB714385A (en) | 1951-07-20 | 1952-07-18 | Purification of acrylonitrile |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB714385A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2770840A1 (en) * | 1997-10-23 | 1999-05-14 | Mitsubishi Rayon Co | Production of amide from nitrile by nitrile hydratase treatment |
WO2004063145A1 (en) * | 2003-01-03 | 2004-07-29 | The Standard Oil Company | Process for recovering acrylonitrile or methacrylonitrile |
-
1952
- 1952-07-18 GB GB18199/52A patent/GB714385A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2770840A1 (en) * | 1997-10-23 | 1999-05-14 | Mitsubishi Rayon Co | Production of amide from nitrile by nitrile hydratase treatment |
WO2004063145A1 (en) * | 2003-01-03 | 2004-07-29 | The Standard Oil Company | Process for recovering acrylonitrile or methacrylonitrile |
US7250527B2 (en) | 2003-01-03 | 2007-07-31 | Ineos Usa Llc | Process for recovering acrylonitrile or methacrylonitrile |
EA009177B1 (en) * | 2003-01-03 | 2007-12-28 | ИНЕОС ЮЭсЭй ЭлЭлСи | Process for recovering acrylonitrile or methacrylonitrile |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3187055A (en) | Manufacture of peroxidic compounds | |
US2653966A (en) | Purification of acrylonitrile | |
GB714385A (en) | Purification of acrylonitrile | |
US2776322A (en) | Manufacture of beta-naphthol | |
GB732800A (en) | Purification of acrylates by distillation | |
US3187050A (en) | Process for conditioning reducible cyclic organic compounds | |
US2361367A (en) | Method of removing acetylene polymers from crude acrylonitrile | |
US2619510A (en) | Manufacture of isopropyl benzene hydroperoxide | |
US2042729A (en) | Separating fatty acids | |
US2560950A (en) | Production of o-cresol derivatives | |
US2197956A (en) | Vapor phase dehydration of acetylenic alcohols | |
US2527680A (en) | Alpha thenyl chloride from hydrogen chloride-formaldehyde solution and thiophene | |
US4491673A (en) | Production and separation of amines | |
US2626959A (en) | Process for extraction of olefinic hydrocarbon mixtures | |
US2417380A (en) | Process for the preparation of alpha-nitro-isobutene | |
US2546431A (en) | Production of vinyl allyl ether | |
KR850002956A (en) | Purification method of fluorocarbon compound | |
DE1276049B (en) | Process for the preparation of acylaminophenols | |
US2311189A (en) | Purification of benzene | |
US2757207A (en) | alpha, alpha-dimethylnaphthylmethyl hydroperoxides | |
US2411225A (en) | 3, 4-dibromotetrahydrothiophene | |
GB579787A (en) | Improvements in or relating to the refining of crude acrylonitrile | |
US2479996A (en) | Synthesis of organic sulfur compounds | |
US1066474A (en) | Process of producing diacetone alcohol. | |
US2761777A (en) | Process for recovering an alkaline earth metal from admixture with an alkali metal |