GB818722A - Improvements in the manufacture of acrylonitrile - Google Patents
Improvements in the manufacture of acrylonitrileInfo
- Publication number
- GB818722A GB818722A GB29526/56A GB2952656A GB818722A GB 818722 A GB818722 A GB 818722A GB 29526/56 A GB29526/56 A GB 29526/56A GB 2952656 A GB2952656 A GB 2952656A GB 818722 A GB818722 A GB 818722A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hcn
- acrylonitrile
- acetaldehyde
- excess
- free
- 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
A crude aqueous acrylonitrile solution containing acetaldehyde, obtained by reacting HCN and acetylene to form an acetylene-bearing gas and scrubbing said gas with water, is refined by distillation, characterized in that a free -HCN content in excess of that stoichiometrically equivalent to the acetaldehyde content is provided in the solution. The acrylonitrile solution obtained from the scrubber may be subjected to steam stripping to concentrate it, a free-HCN content in excess of the acetaldehyde being provided in the concentrated acrylonitrile which is then distilled to produce a purified acrylonitrile product. The amount of excess HCN is not critical and may be provided for in any suitable manner. Preferably the HCN feed to the HCN-acetylene reactor is such as to ensure the required excess. The excess HCN may also be provided by adding sufficient HCN directly prior to, following, or during the steam stripping operation. In examples: (2) illustrates the distillation of a crude wet acrylonitrile containing sufficient free HCN to react with all of the free acetaldehyde; (1) is a comparative example; (3)-(12) illustrate experiments conducted on acrylonitrile solutions containing differing amounts of HCN and acetaldehyde to determine the stability against polymerization, the method utilized being the oxygen bomb induction period method described in Specification 600,708.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US818722XA | 1955-10-05 | 1955-10-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB818722A true GB818722A (en) | 1959-08-19 |
Family
ID=22166938
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB29526/56A Expired GB818722A (en) | 1955-10-05 | 1956-09-27 | Improvements in the manufacture of acrylonitrile |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB818722A (en) |
Cited By (1)
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 |
-
1956
- 1956-09-27 GB GB29526/56A patent/GB818722A/en not_active Expired
Cited By (1)
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 |
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