GB821958A - Purifying acrylonitrile by distillation - Google Patents

Purifying acrylonitrile by distillation

Info

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
Application number
GB29368/56A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wyeth Holdings LLC
Original Assignee
American Cyanamid Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by American Cyanamid Co filed Critical American Cyanamid Co
Publication of GB821958A publication Critical patent/GB821958A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • C07C253/32Separation; Purification; Stabilisation; Use of additives
    • C07C253/34Separation; 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.
GB29368/56A 1955-10-05 1956-09-26 Purifying acrylonitrile by distillation Expired GB821958A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (6)

* Cited by examiner, † Cited by third party
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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