GB290679A - Improved manufacture of concentrated nitric acid - Google Patents
Improved manufacture of concentrated nitric acidInfo
- Publication number
- GB290679A GB290679A GB14769/28A GB1476928A GB290679A GB 290679 A GB290679 A GB 290679A GB 14769/28 A GB14769/28 A GB 14769/28A GB 1476928 A GB1476928 A GB 1476928A GB 290679 A GB290679 A GB 290679A
- Authority
- GB
- United Kingdom
- Prior art keywords
- water
- oxygen
- nitric acid
- nitric oxide
- chambers
- 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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
290,679. Montecatini Soc. GÚnÚrale per l'Industria Mineraria ed Agricola. May 20, 1927, [Convention date]. Void [Published under Sect. 91 of the Acts]. Nitric acid, catalytic production of.- Concentrated nitric acid is obtained by catalytically oxidizing ammonia to produce nitric oxide and water which are then separated from one another, oxidizing the nitric oxide to nitrogen peroxide, absorbing this in a portion of the water, and treating the solution with oxygen. In the illustrated apparatus air and ammonia are mixed at A, compressed at B to 5-6 atmospheres, and passed through a filter C to the contact chamber D. The products are cooled in the heatexchanger E and coil F and passed to the separator I. The nitric oxide is mixed in the chambers H with oxygen from the pipe G and the resulting nitrogen peroxide is absorbed in the water passing through the chambers L. Superfluous water is withdrawn from the system at O. The solution is treated in the column P with compressed oxygen at 40-50‹ C. with production of concentrated acid. Unabsorbed gases after passing through the heat-exchanger, drive an engine S coupled to the compressor B.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT290679X | 1927-05-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB290679A true GB290679A (en) | 1929-03-14 |
Family
ID=11226089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB14769/28A Expired GB290679A (en) | 1927-05-20 | 1928-05-19 | Improved manufacture of concentrated nitric acid |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB290679A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2556835A (en) * | 1945-12-29 | 1951-06-12 | Standard Oil Dev Co | Process for producing gas mixtures |
| US4235858A (en) * | 1978-04-07 | 1980-11-25 | Boc Limited | Processes for producing nitric acid by utilization of cold oxygen |
-
1928
- 1928-05-19 GB GB14769/28A patent/GB290679A/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2556835A (en) * | 1945-12-29 | 1951-06-12 | Standard Oil Dev Co | Process for producing gas mixtures |
| US4235858A (en) * | 1978-04-07 | 1980-11-25 | Boc Limited | Processes for producing nitric acid by utilization of cold oxygen |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2088057A (en) | Production of nitric acid from oxides of nitrogen | |
| GB290679A (en) | Improved manufacture of concentrated nitric acid | |
| ES376742A1 (en) | Process for the production of nitric acid with a concentration of over 70 percent by weight | |
| GB904982A (en) | A process for the preparation of sulphur trioxide | |
| GB434302A (en) | Improvements in or relating to the absorption of nitrogen oxides | |
| JPS61257940A (en) | Production of dicarboxylic acid | |
| US2123467A (en) | Process for the production of highly concentrated nitric acid | |
| GB749645A (en) | Improvements relating to the catalytic oxidation of sulphur dioxide to sulphur trioxide | |
| GB221514A (en) | Improvements in the process of producing ammonium nitrate | |
| US1264512A (en) | Denitration of sulfuric acid. | |
| GB191407419A (en) | Process for the Absorption of Dilute Nitrogenous Gases by Water. | |
| DE593961C (en) | Production of concentrated nitric acid | |
| SU433784A1 (en) | The method of producing adipic acid | |
| GB120378A (en) | Improvements in or relating to the Manufacture of Concentrated Nitric Acid. | |
| US1845413A (en) | Contact method of sulphuric acid manufacture | |
| SU184261A1 (en) | R.A.N.P. Konkov, L.M. Polkova and E.P. Vershig "nal" p; -; 'e-aJBHSKlvfictfA;.' BPB-SOT ^^ pd | |
| ES391519A1 (en) | Method for producing concentrated nitric acid | |
| SU611879A1 (en) | Method of obtaining ammonium nitrite | |
| GB742228A (en) | Process for the manufacture of concentrated phospho-nitric acid | |
| GB636951A (en) | Process of and apparatus for the production of nitric acid | |
| GB172979A (en) | Improvements in the manufacture of nitric acid from the gases obtained through the oxidation of ammonia | |
| JPS5824367B2 (en) | Manufacturing method of ammonium nitrite | |
| SU131344A1 (en) | The method of obtaining nitric acid | |
| GB502155A (en) | Method of oxidation of ammonia | |
| GB363436A (en) | Improvements in or relating to the manufacture of nitric acid from ammonia |