Process for the separation of NH.sub.3 from a gaseous mixture containing NH.sub.3 and HCN

• US 4,094,958 A
• Filed: 04/05/1977
• Issued: 06/13/1978
• Est. Priority Date: 04/05/1977
• Status: Expired due to Term

• Current Assignee: Ciba-Geigy Corporation (Novartis Ag)
• Original Assignee: Ciba-Geigy Corporation (Novartis Ag)
• Inventors: Miller, Ralph
• Primary Examiner(s): Vertiz, O. R.
• Assistant Examiner(s): Wheelock, Eugene T.
• Application Number:
  US05/784,771
• Time in Patent Office: 434 Days
• Field of Search: 423/238, 423/396, 423/236, 55/68, 55/70
• US Class Current: 423/238
• CPC Class Codes: C01C 1/12 Separation of ammonia from gases and vapours as part of the ammonia synthesis process C01C1/04

Abstract

A process for the separation of ammonia from a gaseous mixture containing ammonia and hydrogen cyanide which comprises contacting said gaseous mixture in an absorption stage with an absorbent liquor comprising an acidified ammonium nitrate solution thereby selectively absorbing ammonia from said gaseous mixture and forming a solution of diminished acidity, adding nitric acid to the ammonium nitrate-containing solution of diminished acidity to restore its acidity to its initial level and recycling said restored solution to said absorption stage.

Claims

1. A process for the separation of ammonia from a gaseous mixture containing ammonia and hydrogen cyanide which comprises contacting said gaseous mixture in an absorption stage with an absorbent liquor comprising an acidified ammonium nitrate solution thereby selectively absorbing ammonia from said gaseous mixture and forming a solution of diminished acidity, adding nitric acid to the ammonium nitrate-containing solution of diminished acidity to restore its acidity to its initial level and recycling said restored solution to said absorption stage, said nitric acid being present in the liquid and vapor phase of said ammonium nitrate-containing solution in an amount sufficient to inhibit azulmic acid formation.

2. The process according to claim 1 wherein said absorbent liquor contains 40 to 65% by weight of ammonium nitrate dissolved therein.

3. The process according to claim 1 wherein said absorbent liquor contains about 1% to about 5% nitric acid.

4. The process according to claim 2 wherein said contacting is performed at about 60°

C to about 100°

C.

5. The process according to claim 1 wherein said gaseous mixture contains 0.5 to 5% ammonia and 2% to 16% hydrogen cyanide.

6. The process according to claim 3 wherein said nitric acid concentration is maintained by continuous or periodic addition of nitric acid to said recirculating liquor.

7. The process according to claim 6 wherein the volume of absorbent liquor is controlled by bleeding off a portion of said recirculating liquor periodically or continuously.

8. The process according to claim 1 wherein the said gaseous mixture containing ammonia and hydrogen cyanide is the effluent from the reaction between methane, ammonia and oxygen to produce hydrogen cyanide and water, said effluent also containing unreacted ammonia.