AT49035B - Process for the production of pure nitrate and nitrite by the absorption of nitrous gases. - Google Patents
Process for the production of pure nitrate and nitrite by the absorption of nitrous gases.Info
- Publication number
- AT49035B AT49035B AT49035DA AT49035B AT 49035 B AT49035 B AT 49035B AT 49035D A AT49035D A AT 49035DA AT 49035 B AT49035 B AT 49035B
- Authority
- AT
- Austria
- Prior art keywords
- nitrite
- absorption
- nitrate
- production
- nitrous gases
- Prior art date
Links
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 title claims description 11
- 238000010521 absorption reaction Methods 0.000 title claims description 10
- 239000007789 gas Substances 0.000 title claims description 10
- 229910002651 NO3 Inorganic materials 0.000 title claims description 9
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 title claims description 9
- 238000000034 method Methods 0.000 title claims description 5
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous oxide Inorganic materials [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 title claims description 3
- 238000002425 crystallisation Methods 0.000 claims description 2
- 230000008025 crystallization Effects 0.000 claims description 2
- 230000008020 evaporation Effects 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- LPXPTNMVRIOKMN-UHFFFAOYSA-M sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 235000010288 sodium nitrite Nutrition 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Description
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Verfahren zur Herstellung von reinem Nitrat und Nitrit bei der Absorption von nitrosen Gasen.
Bekanntlich bildet sich, wenn mann feuchte, nicht sehr konzentrierte Gase durch Lösung der Alkalien und Erdalkalien, oder durch Karbonate der Alkalien und Erdalkalien
EMI1.1
Nitrit umsomehr, je dünner die Gase sind.
Man hat diese Reaktion benutzt, um einerseits die Restgase bei der Absorption
EMI1.2
Technisch am wichtigsten ist die Absorption durch Natriumkarbonat, welches einerseits ein gut lösliches und äusserst intensiv wirkeudos Absorptionsmittel darstellt und andererseits das technisch sehr vielseitig verwendete Natriumnitrit liefert.
Ks gelillgt nun aber nicht, das Gemenge von Natriumnitrit und Natriumnitrat voll- ständig in die beiden Komponenten zu zerlegen. d. h. also, beide Salze voneinander zu
EMI1.3
aufgebraucht.
Auf diese Weise kommen natürlich alle Salpetersäuredampfo in der ganzen Lauge zur Absorption und das Nitrat befindet siel) im Gemisch mit sämtlichem gewonnenen Nitrit. Dieser Überlstand wird nun durch das vorliegende neue Verfahren völlig vermieden.
EMI1.4
gleiche Teile Nitrat und Nitrit enthält, wird zum berieselt des ersten Turmes benutzt.
Da in diesem vorwiegend Salpetersäuredämpfe zur Absorption gelangen, so wird
EMI1.5
<Desc/Clms Page number 2>
das Nitrit vollkommen in Nitrat verwandelt und das hieboi freiwerdende Gemisch von NO2 und NO durch die grossen Gasmengen rasch so verdünnt, dass eine weitere Oxydation zu N2 0, nicht erfolgt und das Gas fast vollständig zur Neubildung von Nitrit in der weiteren Absorption nutzbar gemacht wird.
Sowie die Rieselftüssigl (eit im Turm 1 beginnt Säurrreaktion zu zeigen, ist sie erschöpft, d. h. sie enthält nur noch Nitrat und dieses kann in reinem Zustand durch Kristallisation gewonnen werden, während die Mutterlauge auch dieses Prozesses auf den Turm 1 zurückwandert.
Die zweite Abteilung der Absorption ergibt nun sogleich einen bedeutend höheren Nitritgehalt als vorher, und es stellt sich zwischen der Menge des in Turm 1 zersetzten Nitrites und des in der weiteren Absorption mitgewonnenen Prozentsatzes an Nitrat von selbst ein bestimmtes Verhältnis her, das notwendigerweise eintreten muss, weil eben die Löslichkeit der Salze annähernd gleich ist.
<Desc / Clms Page number 1>
Process for the production of pure nitrate and nitrite by the absorption of nitrous gases.
It is well known that when moist, not very concentrated gases are formed by dissolving alkalis and alkaline earths, or by carbonates of alkalis and alkaline earths
EMI1.1
The thinner the gases, the more nitrite.
This reaction was used to remove the residual gases during absorption
EMI1.2
Technically most important is the absorption by sodium carbonate, which on the one hand is a readily soluble and extremely intensely effective absorbent and on the other hand provides the technically very versatile sodium nitrite.
But Ks does not succeed in completely breaking down the mixture of sodium nitrite and sodium nitrate into the two components. d. H. so, both salts of each other too
EMI1.3
used up.
In this way, of course, all the nitric acid vapor in the entire liquor is absorbed and the nitrate is found in a mixture with all the nitrite obtained. This excess is now completely avoided by the present new method.
EMI1.4
Contains equal parts nitrate and nitrite, is used to sprinkle the first tower.
Since mainly nitric acid vapors are absorbed in this, so is
EMI1.5
<Desc / Clms Page number 2>
the nitrite is completely transformed into nitrate and the mixture of NO2 and NO that is released is quickly diluted by the large amounts of gas so that further oxidation to N2 0 does not take place and the gas is almost completely usable for the formation of new nitrite in further absorption.
As soon as the trickle liquid begins to show an acid reaction in tower 1, it is exhausted, i.e. it only contains nitrate and this can be obtained in a pure state through crystallization, while the mother liquor also migrates back to tower 1 in this process.
The second division of absorption now immediately results in a significantly higher nitrite content than before, and a certain ratio is automatically established between the amount of nitrite decomposed in tower 1 and the percentage of nitrate gained in further absorption, which must necessarily occur, because the solubility of the salts is approximately the same.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT49035T | 1910-09-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT49035B true AT49035B (en) | 1911-07-25 |
Family
ID=3569694
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT49035D AT49035B (en) | 1910-09-27 | 1910-09-27 | Process for the production of pure nitrate and nitrite by the absorption of nitrous gases. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT49035B (en) |
-
1910
- 1910-09-27 AT AT49035D patent/AT49035B/en active
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