GB821958A - Purifying acrylonitrile by distillation - Google Patents
Purifying acrylonitrile by distillationInfo
- Publication number
- GB821958A GB821958A GB29368/56A GB2936856A GB821958A GB 821958 A GB821958 A GB 821958A GB 29368/56 A GB29368/56 A GB 29368/56A GB 2936856 A GB2936856 A GB 2936856A GB 821958 A GB821958 A GB 821958A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acrylonitrile
- solution
- hcn
- lactonitrile
- stripping
- 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
Acrylonitrile is obtained from a dilute aqueous solution thereof, which contains lactonitrile as an impurity, by subjecting the solution to steam-stripping while maintaining the pH of the solution at about 6 to 9 by addition of an hydroxide, phosphate, borate, or carbonate of an alkali or alkaline-earth metal, or a corresponding ammonium compound. Under these conditions the lactonitrile is dissociated into acetaldehyde and hydrogen cyanide; and these compounds distil over with the acrylonitrile, so that the residue may safely be discharged to waste. On condensation, the distillate stratifies into a water layer and an acrylonitrile layer. The water layer may be returned as reflux to the stripping column. The acrylonitrile layer, which contains acetaldehyde and hydrogen cyanide, is further treated to obtain a pure product. In an example, an aqueous acrylonitrile solution, obtained by water-scrubbing a gas from the reaction of HCN with acetylene, and having a total HCN concentration of 2140 p.p.m. of which 1140 p.p.m. is as free HCN and the remainder is in the form of lactonitrile, is adjusted to a pH of 6.3 by the addition of 0.5N caustic soda. The solution is then stripped with steam over a period of 20 minutes at 100 DEG C. After stripping, the concentration of HCN in the column-bottoms, either in the form of lactonitrile or as free HCN, is found to be only 78 p.p.m.ALSO:Acrylonitrile is obtained from a dilute aqueous solution thereof, which contains lactonitrile as an impurity, by subjecting the solution to steam-stripping while maintaining the pH of the solution at about 6 to 9 by addition of an hydroxide, phosphate, borate or carbonate of an alkali or alkaline-earth metal, or a corresponding ammonium compound. Under these conditions the lactonitrile is dissociated into acetaldehyde and hydrogen cyanide; and these compounds distil over with the acrylonitrile, so that the residue may be safely discharged to waste. On condensation, the distillate stratifies into a water layer and an acrylonitrile layer. The water layer may be returned as reflux to the stripping column. The acrylonitrile layer, which contains acetaldehyde and hydrogen cyanide, is further treated to obtain a pure product. In an example, an aqueous acrylonitrile solution, obtained by water-scrubbing a gas from the reaction of HCN with acetylene, and having a total HCN concentration of 2140 p.p.m. of which 1140 p.p.m. is as free HCN and the remainder is in the form of lactonitrile, is adjusted to a pH of 6.3 by addition of 0.5 N caustic soda. The solution is then stripped with steam for 20 minutes. After stripping, the total concentration of HCN in the column-bottoms is only 78 p.p.m.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US821958XA | 1955-10-05 | 1955-10-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB821958A true GB821958A (en) | 1959-10-14 |
Family
ID=22169643
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB29368/56A Expired GB821958A (en) | 1955-10-05 | 1956-09-26 | Purifying acrylonitrile by distillation |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB821958A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1288597B (en) * | 1963-01-16 | 1969-02-06 | Knapsack Ag | Process for the production of pure acrylic acid nitrile and pure hydrogen cyanide from crude acrylic acid nitrile |
EP0110861A1 (en) * | 1982-11-22 | 1984-06-13 | Monsanto Company | Process for removal of acrolein from acrylonitrile product streams |
WO2004063145A1 (en) * | 2003-01-03 | 2004-07-29 | The Standard Oil Company | Process for recovering acrylonitrile or methacrylonitrile |
-
1956
- 1956-09-26 GB GB29368/56A patent/GB821958A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1288597B (en) * | 1963-01-16 | 1969-02-06 | Knapsack Ag | Process for the production of pure acrylic acid nitrile and pure hydrogen cyanide from crude acrylic acid nitrile |
EP0110861A1 (en) * | 1982-11-22 | 1984-06-13 | Monsanto Company | Process for removal of acrolein from acrylonitrile product streams |
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 |
CN100338033C (en) * | 2003-01-03 | 2007-09-19 | 标准石油公司 | Process for recovering acrylonitrile or methacrylonitrile |
EA009177B1 (en) * | 2003-01-03 | 2007-12-28 | ИНЕОС ЮЭсЭй ЭлЭлСи | Process for recovering acrylonitrile or methacrylonitrile |
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