BE354613A - - Google Patents
Info
- Publication number
- BE354613A BE354613A BE354613DA BE354613A BE 354613 A BE354613 A BE 354613A BE 354613D A BE354613D A BE 354613DA BE 354613 A BE354613 A BE 354613A
- Authority
- BE
- Belgium
- Prior art keywords
- nitrate
- towers
- absorption
- solution
- mother liquor
- Prior art date
Links
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 7
- 238000010521 absorption reaction Methods 0.000 claims description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 3
- 238000002425 crystallisation Methods 0.000 claims description 3
- 230000005712 crystallization Effects 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 150000002823 nitrates Chemical class 0.000 claims description 3
- IOVCWXUNBOPUCH-UHFFFAOYSA-M nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims 2
- 239000012452 mother liquor Substances 0.000 claims 2
- 241000282326 Felis catus Species 0.000 claims 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims 1
- 150000001342 alkaline earth metals Chemical class 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 150000002500 ions Chemical class 0.000 claims 1
- 238000001704 evaporation Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- SFDJOSRHYKHMOK-UHFFFAOYSA-N Nitramide Chemical compound N[N+]([O-])=O SFDJOSRHYKHMOK-UHFFFAOYSA-N 0.000 description 1
- 235000015450 Tilia cordata Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 229910001963 alkali metal nitrate Inorganic materials 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous oxide Inorganic materials [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000001184 potassium carbonate Substances 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
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
- C01B21/38—Nitric acid
- C01B21/46—Purification; Separation ; Stabilisation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Description
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Procédé de fabrication de nitrates des métaux alcalins et
EMI1.1
alaalino-terreux<.
C'est un fait connu que l'on peut fabriquer des nitrates de potassium, de sodium, de calcium, etc., en faisant ruisse- ler dans les tours d'absorption d'une fabrique d'acide nitri- que des solutions ou des suspensions des hydrates ou des car'- bonates correspondants.
On se sert de ce procédé pour recueillir les dernières quantités de gaz nitreux lors de la fabrication d'acide ni- trique, on obtient ainsi une solution relativement diluée de nitrate, qui contient un peu de nitrite et qui est d'abord débarrassée de sa teneur en nitrile par traitement au moyen @
<Desc/Clms Page number 2>
d'acide nitrique et de vapeur, et est ensuite évaporée en vue de la cristallisation.
Ce procédé est incommode en ce qu'il implique une évapo- ration de solutions de nitrate :les solutions de nitrate at- taquent la matière de l'évaporateur et l'évaporation provo- que une perte nullement négligeable en azote.
Suivant la présente invention, le nitrate est obtenu sous la forme solide sans évaporation.
Le procédé est basé sur la grande différence, de solubi- lité des nitrates à des températures différentes.
En pratique, pour la réalisation du procédé, on refroidit fortement la solution de nitrate exempte de nitrite obtenue, par exemple jusqu'à O C, opération au cours de laquelle la plus grande partie du nitrate se sépare par cristallisation, et après que la lessive-mère a été portée de nouveau à une température convenant pour l'absorption - environ 15 ou 20 - elle est mélangée à de nouvelles quantités du sel alcalin ou alcalino-terreux envisagé - carbonate de soude, carbonate de potasse, hydrate de chaux, etc, La solution fraiche d'alcali ainsi obtenue, qui contient relativement peu de nitrate, est de nouveau saturée au moyen d'amide nitrique par ruisselle- ment dans les tours et après la transformation du nitrite qui y est contenu en nitrate, elle est débarrassée comme plus haut, par refroidissement, de la plus grande partie de son nitrate.
On fait avantageusement chauffer la solutmon froide pau- vre en nitrate par la solution plus chaude riche en nitrate, suivant le principe du contre-courant, de sorte que la solu- tion riche en nitrate se refroidit. Les quantités de chaleur qui doivent être extraites par refroidissement artificiel deviennent ainsi relativement petites et le procédé est donc rendu moins coûteux,
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Manufacturing process of alkali metal nitrates and
EMI1.1
alaalino-earthy <.
It is a known fact that nitrates of potassium, sodium, calcium, etc., can be made by roasting in the absorption towers of a nitric acid factory solutions or suspensions of the corresponding hydrates or carbohydrates.
This process is used to collect the last quantities of nitrous gas during the manufacture of nitric acid, thus obtaining a relatively dilute solution of nitrate, which contains a little nitrite and which is first freed of its substance. nitrile content by treatment with @
<Desc / Clms Page number 2>
nitric acid and vapor, and is then evaporated for crystallization.
This process is inconvenient in that it involves an evaporation of nitrate solutions: the nitrate solutions attack the material of the evaporator and the evaporation causes by no means negligible loss of nitrogen.
According to the present invention, the nitrate is obtained in the solid form without evaporation.
The process is based on the great difference in the solubility of nitrates at different temperatures.
In practice, for carrying out the process, the nitrite-free nitrate solution obtained is strongly cooled, for example to OC, an operation during which most of the nitrate separates out by crystallization, and after the lye- The mother has been brought again to a temperature suitable for absorption - about 15 or 20 - it is mixed with further quantities of the envisaged alkali or alkaline earth salt - soda ash, potassium carbonate, hydrate of lime, etc., The fresh alkali solution thus obtained, which contains relatively little nitrate, is again saturated with nitric amide by trickling through the towers and after the conversion of the nitrite contained therein into nitrate, it is discarded as higher, by cooling, most of its nitrate.
The cold nitrate-poor solution is advantageously heated by the hotter nitrate-rich solution, according to the countercurrent principle, so that the nitrate-rich solution cools. The quantities of heat which must be extracted by artificial cooling thus become relatively small and the process is therefore made less expensive,
Claims (1)
Publications (1)
Publication Number | Publication Date |
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BE354613A true BE354613A (en) |
Family
ID=29015
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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BE354613D BE354613A (en) |
Country Status (1)
Country | Link |
---|---|
BE (1) | BE354613A (en) |
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0
- BE BE354613D patent/BE354613A/fr unknown
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