BE372062A - - Google Patents
Info
- Publication number
- BE372062A BE372062A BE372062DA BE372062A BE 372062 A BE372062 A BE 372062A BE 372062D A BE372062D A BE 372062DA BE 372062 A BE372062 A BE 372062A
- Authority
- BE
- Belgium
- Prior art keywords
- potassium
- solution
- ammonium
- potassium nitrate
- carbonate
- Prior art date
Links
- FGIUAXJPYTZDNR-UHFFFAOYSA-N Potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 35
- 235000010333 potassium nitrate Nutrition 0.000 claims description 18
- 239000004323 potassium nitrate Substances 0.000 claims description 17
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 10
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 10
- OTYBMLCTZGSZBG-UHFFFAOYSA-L Potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 9
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 9
- 239000011591 potassium Substances 0.000 claims description 9
- 229910052700 potassium Inorganic materials 0.000 claims description 9
- 235000011151 potassium sulphates Nutrition 0.000 claims description 9
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 8
- 235000019270 ammonium chloride Nutrition 0.000 claims description 7
- 239000010440 gypsum Substances 0.000 claims description 7
- 229910052602 gypsum Inorganic materials 0.000 claims description 7
- QDHHCQZDFGDHMP-UHFFFAOYSA-N monochloramine Chemical compound ClN QDHHCQZDFGDHMP-UHFFFAOYSA-N 0.000 claims description 7
- 239000001120 potassium sulphate Substances 0.000 claims description 7
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 6
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 6
- 229960003563 Calcium Carbonate Drugs 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 5
- PRKQVKDSMLBJBJ-UHFFFAOYSA-N Ammonium carbonate Chemical compound N.N.OC(O)=O PRKQVKDSMLBJBJ-UHFFFAOYSA-N 0.000 claims description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 3
- 238000000354 decomposition reaction Methods 0.000 claims description 3
- 239000001103 potassium chloride Substances 0.000 claims description 3
- 235000011164 potassium chloride Nutrition 0.000 claims description 3
- 239000001099 ammonium carbonate Substances 0.000 claims description 2
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 1
- YFRBJGMVZVZRCM-UHFFFAOYSA-N diazanium;carbonate;hydrochloride Chemical compound [NH4+].[NH4+].Cl.[O-]C([O-])=O YFRBJGMVZVZRCM-UHFFFAOYSA-N 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 239000008247 solid mixture Substances 0.000 claims 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 4
- 235000011130 ammonium sulphate Nutrition 0.000 description 4
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N Calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 3
- 239000001166 ammonium sulphate Substances 0.000 description 3
- XKUUMWKWUZRRPD-UHFFFAOYSA-N heptan-2-amine;sulfuric acid Chemical compound [O-]S([O-])(=O)=O.CCCCCC(C)[NH3+].CCCCCC(C)[NH3+] XKUUMWKWUZRRPD-UHFFFAOYSA-N 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- 229910052925 anhydrite Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N Ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229960005069 Calcium Drugs 0.000 description 1
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- -1 ammonium-chlorine ammonium carbonate Chemical compound 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 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)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
<Desc/Clms Page number 1>
EMI1.1
" Procédé pour la fabrication da nitrate de potassium"
EMI1.2
Une méthode COJVt1,-lLe. p C!li' la préparation du nitrate de potassium est la décomposition du sulfate de potas- sium par le nitrate de calcium.
EMI1.3
K2S04 + Ca (id03)2 = Kli03 + CaBo 4
Le gypse formé est séparé de la solution de nitra- te de potassiani par décantage ou filtrage et la solo.- tion obtenue de nitrate de potassium est évaporée.
Cette méthode de fabriquer le nitrate de potas- siam apparait très simple et pleine de promesses,mais elle présente des inconvénients graves.
D'abord la réaction ne se produit pas d'une maniè- re si simple, que l'on le suppose d'après l'équation ci-dessus, parce qu'il ne se forme pas seulement du gypse , mais aussi des co..posés doubles de potassium et de calciam avec l'acide sulfurique, comme la syngeri-
EMI1.4
te ( KSS04. CaS04 . H20 ) et du sulfate de pota ss illm
<Desc/Clms Page number 2>
ponta salfate de calcium ( K2SO4. 5 CaSO4.H2O). Ce- la entraîne des pertes en potasse, qui renchérissent le procédé et le rendent moins avantageux ou défi- citaire .
Un autre inconvénient est qae le sulfate de po- tassiam en lui-même est une matière brate trop chère pour la fabrication du. nitrate de potassium, surtout lorsque ce nitrate de potassium doit être employé comme engrais.
La présente invention se rapporte à an procédé qui permet d'employer la réaction ci-dessus pour la fabrication du salpêtre potassique, sans que les in- convénients mentionnés se produisant,
D'après cette invention on n'emploie pas le sal- fate de potassium, reis le chlorura de potassium, uonuiie matière brute . Elle représente an procédé en circuit fermé, dans lequel le chlorure de potassium, l'acide nitrique, l'acide carbonique, et l'ammoniaque sont employés comme matières brutes et le nitrate de po- tassium et le chlorure d'ammonium représentent les produits finis .
Le procédé est réalisé de la manière suivante:
Dans une solution de chlorure d'ammonium conte- nant du sulfate d'ammonium on brasse une quantité de chlorure de potassium équivalente au salfate d'ammonium et on y dirige de l'ammoniaque. Il seforme du sulfate de potassium comme précipité dans une solution ammonia- cale de chlorure d'ammonium. Le salfate de potassium est séparé des eaux-mères et brassé avec le carbonate de calcium provenait du procédé et de l'acide nitrique, il se forme alors du gypse contenant du sulfate de po-
<Desc/Clms Page number 3>
tassiam et une solution de nitrate do potassiam. On sépare ceux-ci par le décantage ou le filtrage et la solution est évaporée poar obtenir du nitrate de potas- sium solide.
Au lien d'évaporer la solution de nitrate de potas- sium on peut la refroidir pour séparer la plas grande partie du nitrate de potassiam, et employer les eaux- mères poar dissoudre les nouvellesquantités de sulfa- te de potassiam obtenues ensuite.
Les eaax-mères du salfate de potassium sont en- suite refroidis pour séparer une partie du chlorure d'ammonium et après avoir séparé celui-ci, on les satu- re d'acide carbonique pour former du carbonate d'ammo- nium.
Dans cette solution de carbonate da'mmonium-chlo- rare d'ammonium on brasse le gypse contenant du salfate de'patassiam obtenu dans la préparation du nitrate de potassium, ce qui le décompose en sulfate d'ammonium et carbonate de calciam. Cette solation est celle men- tionnée aa commencement comme solution de chlorare d'am- moniam contenant du sulfate d'ammonium dans laquelle on sépare en brassant le chlorare de potassium en y fai- sant passer de l'ammon iaque, ce qui conduit à la for- mation de nouvelles qaantités de sulfate de potassium.
Il n'est pas nécessaire de séparer le carbonate de calcium de la solution de chlorure d'ammonium conte- nant da sulfate d'ammonium, parce que le salfate de potassiam doit être mélangé avec le carbonate de cal- ciam avant sa décomposition par l'acide nitrique.
<Desc / Clms Page number 1>
EMI1.1
"Process for the manufacture of potassium nitrate"
EMI1.2
A method COJVt1, -lLe. The preparation of potassium nitrate is the decomposition of potassium sulphate by calcium nitrate.
EMI1.3
K2S04 + Ca (id03) 2 = Kli03 + CaBo 4
The gypsum formed is separated from the potassium nitrate solution by decanting or filtering and the resulting potassium nitrate solution is evaporated.
This method of making potas- siam nitrate appears very simple and full of promise, but it has serious drawbacks.
In the first place, the reaction does not take place in such a simple way as one supposes from the above equation, because not only gypsum is formed, but also co ..double exposures of potassium and calciam with sulfuric acid, like syngeri-
EMI1.4
te (KSS04. CaS04. H20) and potassium sulphate ss illm
<Desc / Clms Page number 2>
ponta calcium salfate (K2SO4.5 CaSO4.H2O). This leads to losses of potash, which increase the cost of the process and make it less advantageous or loss-making.
Another drawback is that the potassium sulfate itself is too expensive a brate material for the manufacture of. potassium nitrate, especially when this potassium nitrate is to be used as a fertilizer.
The present invention relates to a process which makes it possible to employ the above reaction for the manufacture of potassium saltpeter, without the mentioned drawbacks occurring,
According to this invention, no potassium salpate, only potassium chlorura, a raw material is employed. It represents a closed loop process, in which potassium chloride, nitric acid, carbonic acid, and ammonia are used as raw materials and potassium nitrate and ammonium chloride represent the products. finished.
The process is carried out as follows:
In an ammonium chloride solution containing ammonium sulphate, a quantity of potassium chloride equivalent to ammonium salfate is stirred and ammonia is directed therein. Potassium sulphate is formed as a precipitate in ammonia solution of ammonium chloride. The potassium salfate is separated from the mother liquors and mixed with the calcium carbonate obtained from the process and the nitric acid, it then forms gypsum containing sulphate of po-
<Desc / Clms Page number 3>
tassiam and a solution of potassium nitrate. These are separated by decanting or filtering and the solution is evaporated to obtain solid potassium nitrate.
Instead of evaporating the solution of potassium nitrate, it can be cooled to separate the large part of the potassium nitrate, and use the mother liquors to dissolve the new quantities of potassium sulfate obtained afterwards.
The potassium salfate mothers are then cooled to separate some of the ammonium chloride and after separating this, they are saturated with carbonic acid to form ammonium carbonate.
In this solution of ammonium-chlorine ammonium carbonate, the gypsum containing de-patassiam salfate obtained in the preparation of potassium nitrate is brewed, which decomposes it into ammonium sulphate and calciam carbonate. This solation is that mentioned at the beginning as a solution of ammonium chlorare containing ammonium sulphate in which the potassium chlorare is separated by stirring by passing it through ammonia, which leads to the formation of new quantities of potassium sulphate.
It is not necessary to separate the calcium carbonate from the ammonium chloride solution containing ammonium sulfate, because the potassium salfate must be mixed with the calciam carbonate before its decomposition by the 'nitric acid.
Claims (1)
Publications (1)
Publication Number | Publication Date |
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BE372062A true BE372062A (en) |
Family
ID=43225
Family Applications (1)
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Country Status (1)
Country | Link |
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BE (1) | BE372062A (en) |
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- BE BE372062D patent/BE372062A/fr unknown
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