DE407617C - Process for the production of nitric acid from nitrous gases - Google Patents
Process for the production of nitric acid from nitrous gasesInfo
- Publication number
- DE407617C DE407617C DEF53571D DEF0053571D DE407617C DE 407617 C DE407617 C DE 407617C DE F53571 D DEF53571 D DE F53571D DE F0053571 D DEF0053571 D DE F0053571D DE 407617 C DE407617 C DE 407617C
- Authority
- DE
- Germany
- Prior art keywords
- nitric acid
- production
- nitrous gases
- water
- nitrous
- 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
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/20—Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
- C01B21/24—Nitric oxide (NO)
- C01B21/26—Preparation by catalytic or non-catalytic oxidation of ammonia
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Description
Verfahren zur Herstellung von Salpetersäure aus nitrosen Gasen. Bei Verarbeitung nitroser Gase auf w<ißrige Salpetersäure kommt man bei den bekannten Verfahren der Berieselung mit Wasser auf eine Salpetersäure, welche im praktischen Betrieb etwa 5o bis 55 Prozent enthält. Versuche von F ö r s t e r , Z. f. angew. Chemie, Band 33, 1920, S. i i 3, 122, 129 haben gezeigt, daß man so im Maximum zu einer Säure von 7oProzent kommen kann, dies jedoch unterBedingungen,welche sich impraktischen Großbetrieb nicht verwirklichen lassen, weil die Reaktionsgeschwindigkeit mit steigender Säurekonzentration stark abnimmt.Process for the production of nitric acid from nitrous gases. When processing nitrous gases to aqueous nitric acid, the known methods of sprinkling with water result in nitric acid which in practical operation contains about 50 to 55 percent. Attempts by F ö rster, f Z. Angew.. Chemie, Volume 33, 1 920, p ii 3, 122, 129 have shown that one can get so at the maximum to an acid of 7oProzent, this, however, under conditions which extends Do not allow impractical large-scale operations to be realized because the rate of reaction decreases sharply with increasing acid concentration.
Es wurde nun die Beobachtung gemacht. claß man unter Vermittlung adsorbier ender Substanzen durch Einwirken von Sauerstoff bzw. Luft und Wasser auf adsorbierte Nitrose leicht zu wesentlich höher konzentrierter Salpetersäure kommen kann.The observation was now made. one must adsorb through mediation ender substances by the action of oxygen or air and water on adsorbed Nitrose can easily lead to significantly higher concentrated nitric acid.
Beispielsweise kann bei Anwendung von Iiieselsäuregel als Adsorbens und Zugabe des nötigen Wassers als solches. bei Oxydation mit Luft eine Säure von 8o Prozent durch Austreiben in der Hitze gewonnen werden. Bei anderen Versuchen wurden Säuren bis zu 9o Prozent Gehalt an Salpetersäure erhalten.For example, when using silicic acid gel as an adsorbent and adding the necessary water as such. when oxidized with air an acid of 80 percent can be obtained by expelling in the heat. With other attempts Acids with a nitric acid content of up to 90 percent were obtained.
Man kann natürlich auch so verfahren, daß man Sauerstoff (auch in Form von Luft) mit Wasserdampf vermischt über das Adsorbat leitet oder bei der Adsorption von Nitrose und Sauerstoff enthaltenden Gasen Wasserdampf oder Wasser in entsprechenden Mengen zugibt.You can of course also proceed in such a way that oxygen (also in Form of air) mixed with water vapor passes over the adsorbate or during adsorption of nitrous and oxygen-containing gases water vapor or water in corresponding Admits quantities.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEF53571D DE407617C (en) | 1923-02-26 | 1923-02-27 | Process for the production of nitric acid from nitrous gases |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE211845X | 1923-02-26 | ||
DEF53571D DE407617C (en) | 1923-02-26 | 1923-02-27 | Process for the production of nitric acid from nitrous gases |
Publications (1)
Publication Number | Publication Date |
---|---|
DE407617C true DE407617C (en) | 1924-12-19 |
Family
ID=25760974
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEF53571D Expired DE407617C (en) | 1923-02-26 | 1923-02-27 | Process for the production of nitric acid from nitrous gases |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE407617C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2756127A (en) * | 1952-06-30 | 1956-07-24 | Union Oil Co | Chemical oxidation process in the adsorbed phase |
-
1923
- 1923-02-27 DE DEF53571D patent/DE407617C/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2756127A (en) * | 1952-06-30 | 1956-07-24 | Union Oil Co | Chemical oxidation process in the adsorbed phase |
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