AT125184B - Process for the production of nitric acid. - Google Patents
Process for the production of nitric acid.Info
- Publication number
- AT125184B AT125184B AT125184DA AT125184B AT 125184 B AT125184 B AT 125184B AT 125184D A AT125184D A AT 125184DA AT 125184 B AT125184 B AT 125184B
- Authority
- AT
- Austria
- Prior art keywords
- nitric acid
- production
- ammonia
- oxidation
- usual
- Prior art date
Links
Landscapes
- Treating Waste Gases (AREA)
Description
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Verfahren zur Herstellung von Salpetersäure.
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Die über die Schalenränder überlaufende Flüssigkeit zirkuliert in den untenliegenden Kammern, während die emporsteigenden Gase durch die Flüssigkeit gurgeln. Unter diesen Verhältnissen gehen die
Stiekstoffoxyde wegen der niedrigen Temperatur und des hohen Drucks vollständig in Lösung auf.
Die restlichen Gase verlassen die Absorptionssäule über die Auslassventile M.
Die am Boden der Säule L abfliessende Flüssigkeit ist verdünnte, Stickstoffoxyde in Lösung. szu- stand enthaltende Salpetersäure. Dieselbe wird der Reaktionssäule N zugeführt, worin sie auf 50 -60 C erwärmt, und mit dem durch den Hahn 0 zufliessenden verdichteten Sauerstoff in Berührung gebracht wird.
Unter diesen Umständen reagieren die gelösten Stickstoffoxyde mit dem restlichen Wasser, wobei sich konzentrierte Salpetersäure bildet. Die Salpetersäure kann man mittels des Hahnes P entnehmen,
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Process for the production of nitric acid.
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The liquid overflowing the bowl rim circulates in the chambers below, while the rising gases gurgle through the liquid. Under these circumstances they go
Oxides of nitrogen completely in solution because of the low temperature and high pressure.
The remaining gases leave the absorption column via the outlet valves M.
The liquid flowing off at the bottom of column L is dilute nitrogen oxides in solution. nitric acid containing the state. The same is fed to the reaction column N, in which it is heated to 50-60 ° C. and is brought into contact with the compressed oxygen flowing in through the tap 0.
Under these circumstances the dissolved nitrogen oxides react with the remaining water to form concentrated nitric acid. The nitric acid can be taken from the tap P,
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Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT125184X | 1929-02-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
AT125184B true AT125184B (en) | 1931-10-26 |
Family
ID=11141103
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AT125184D AT125184B (en) | 1929-02-27 | 1929-10-22 | Process for the production of nitric acid. |
Country Status (1)
Country | Link |
---|---|
AT (1) | AT125184B (en) |
-
1929
- 1929-10-22 AT AT125184D patent/AT125184B/en active
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