CH98564A - Process for the manufacture of a fertilizer based on urea nitrate from cyanamide. - Google Patents
Process for the manufacture of a fertilizer based on urea nitrate from cyanamide.Info
- Publication number
- CH98564A CH98564A CH98564DA CH98564A CH 98564 A CH98564 A CH 98564A CH 98564D A CH98564D A CH 98564DA CH 98564 A CH98564 A CH 98564A
- Authority
- CH
- Switzerland
- Prior art keywords
- nitrate
- cyanamide
- solution
- urea
- manufacture
- Prior art date
Links
- XZMCDFZZKTWFGF-UHFFFAOYSA-N Cyanamide Chemical compound NC#N XZMCDFZZKTWFGF-UHFFFAOYSA-N 0.000 title claims description 16
- QHDUJTCUPWHNPK-UHFFFAOYSA-N methyl 7-methoxy-2h-indazole-3-carboxylate Chemical compound COC1=CC=CC2=C(C(=O)OC)NN=C21 QHDUJTCUPWHNPK-UHFFFAOYSA-N 0.000 title claims description 11
- 238000000034 method Methods 0.000 title claims description 8
- 239000003337 fertilizer Substances 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 9
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 9
- 239000004571 lime Substances 0.000 claims description 9
- 229910002651 NO3 Inorganic materials 0.000 claims description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 6
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 claims description 3
- 230000008020 evaporation Effects 0.000 claims description 3
- 229910021653 sulphate ion Inorganic materials 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims description 2
- LQHXWZKKJHDWRJ-UHFFFAOYSA-O diazanium hydrogen sulfate nitrate Chemical compound [NH4+].[NH4+].[O-][N+]([O-])=O.OS([O-])(=O)=O LQHXWZKKJHDWRJ-UHFFFAOYSA-O 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 239000000243 solution Substances 0.000 description 12
- 239000000203 mixture Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 2
- 235000011130 ammonium sulphate Nutrition 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 239000001166 ammonium sulphate Substances 0.000 description 1
- PRORZGWHZXZQMV-UHFFFAOYSA-N azane;nitric acid Chemical compound N.O[N+]([O-])=O PRORZGWHZXZQMV-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001912 cyanamides Chemical class 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 239000011505 plaster Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 1
- 229910052939 potassium sulfate Inorganic materials 0.000 description 1
- 239000001120 potassium sulphate Substances 0.000 description 1
- 235000011151 potassium sulphates Nutrition 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
Landscapes
- Fertilizers (AREA)
Description
Procédé pour la fabrication d'un engrais à base de nitrate d'ui à partir de la cyanamide. Pour préparer le nitrate d'urée dont on peut se servir pour la préparation d'engrais à partir des cyanamides, on traite générale ment la cyanamide libre en solution aqueuse par l'acide nitrique. L'acide transforme la cyanamide en urée et cette dernière en ni trate d'urée difficilement soluble.
Les principaux défauts de ce procédé sont suivants: 1 Les solutions de cyanamide libre, généralement fort étendues, doivent être cou- centrées par évaporation, soit à la pression ordinaire, soit dans le vide. Selon un récent brevet relatif à cette préparation, la concen tration doit être poussée jusqu'à une consis tance sirupeuse. Or, il est impossible d'éva porer économiquement des solutions aqueuses de cyanamide, cette substance étant volatile avec les vapeurs d'eau et, en outre, très su jette à la polymérisation.
Les rendements en cyanamide devenant ainsi fort défectueux, il va sans dire que la production de nitrate d'urée doit en subir les conséquences. 20 L'acide nitrique étant un acide rela tivement cher, -il est évident que toute pré paration basée sur l'emploi de ce produit doit pouvoir supporter des frais élevés en matière première.
Le procédé qui fait l'objet de la présente invention a pour but de parer à ces incon vénients, Selon ce procédé,- on prépare une solution concentrée de cyanamide en évitant toute évaporation et l'on transforme cette solution en un engrais à base de nitrate d'urée par addition d'acide sulfurique et d'un nitrate en quantité équivalente à cët acide. Ce nitrate peut être par exemple un nitrate alcalin (sodium, potassium), le nitrate d'ammonium, un nitrate d'un métal alcalino-terreux (cal cium, magnésium) etc.
Pour la mise en oruvre de ce procédé, on peut, par exemple, opérer de la manière sui vante: On décompose d'abord la chaux azotée par l'acide carbonique en présence d'eau et l'on obtient une solution de cyanamide. libre que l'on filtre pour la débarrasser du car bonate de chaux, de charbon et d''autres im puretés insolubles.
On répète cette opération avec la solution filtrée qui ressert ainsi à des extractions successives, afin de pouvoir ob tenir une aussi grande concentration que possible de cyanamide. Vu l'instabilité des solutions concentrées de ce corps, surtout en présence de bases faibles, on doit avoir soin d'éviter un contact prolongé des solutions avec la chaux azotée; il est, d'autre part, nécessaire de débarrasser le résidu, d'une façon complète, de toute trace de cyanamide libre, retenue par le charbon et le carbonate de chaux.
Pour arriver à ces résultats sans compromettre le but recherché, on surveillera les solutions qui servent aux extractions mul tiples, en ayant soin de les aciduler faible ment par l'adjonction de petites quantités d'acide ou en les gardant à l'abri de l'air c'est-à-dire dans une atmosphère d'anhy dride carbonique que l'on introduira si pos sible sous pression.
La solution concentrée de cyanamide ob tenue est additionnée d'acide sulfurique à 53 ou<B>600</B> B et d'une quantité correspondante de nitrate alcalin, ammoniacal, magnésien etc.
On laisse reposer pendant la nuit et l'on réchauffe le mélange au bain-marie jusqu'à la disparition complète de la cyanamide libre, ce qui nécessite généralement une à deux heures.
Le nitrate d'urée formé se dépose à froid en cristaux pailletés transparents et peut éventuellement être séparé du sulfate d'am monium, potassium, magnésium etc. par fil tration.
Le mélange de nitrate d'urée et de sul fate d'ammonium ou de potassium pourra souvent servir tel quel comme engrais après avoir été débarrassé de tout excès d'humidité sans séparation préalable.
Vu le fait que l'acide qui sert à la trans formation de la cyanamide peut être employé dans certaines limites en quantités variables, on peut également obtenir des mélanges con tenant de l'urée libre et du nitrate d'urée, ou bien de l'urée, du nitrate d'urée et des sulfates alcalins, ammoniacaux, magnésiens etc.
Le sulfate d'ammonium en solution, séparé par filtration des cristaux de nitrate d'urée, comme décrit ci-dessus, peut être transformé de nouveau en nitrate d'ammonium par traite ment de la solution concentrée par le nitrate de chaux. Le sulfate de chaux se précipite et absorbe deux molécules d'eau en se trans formant en plâtre. Le nitrate d'ammoniaque en solution très concentrée est évaporé à sec et peut resservir à nouveau. On peut égale ment sécher directement le mélange de sul fate de chaux et de nitrate d'ammoniaque obtenu comme produit secondaire et l'employer tel quel comme engrais dans l'agi-ictiltui,e.
Process for the manufacture of a fertilizer based on ui nitrate from cyanamide. In order to prepare urea nitrate which can be used for the preparation of fertilizers from cyanamides, the free cyanamide in aqueous solution is generally treated with nitric acid. The acid converts cyanamide into urea and the latter into hardly soluble urea nitrate.
The main drawbacks of this process are as follows: 1 The solutions of free cyanamide, generally very large, must be offset by evaporation, either at ordinary pressure or in a vacuum. According to a recent patent relating to this preparation, the concentration must be pushed to a syrupy consistency. However, it is impossible to economically eva pore aqueous solutions of cyanamide, this substance being volatile with water vapors and, moreover, very prone to polymerization.
The cyanamide yields thus becoming highly defective, it goes without saying that the production of urea nitrate must suffer the consequences. Since nitric acid is a relatively expensive acid, it is obvious that any preparation based on the use of this product must be able to withstand high raw material costs.
The object of the process which is the subject of the present invention aims to overcome these drawbacks, According to this process, - a concentrated solution of cyanamide is prepared while avoiding any evaporation and this solution is transformed into a fertilizer based on urea nitrate by adding sulfuric acid and a nitrate in an amount equivalent to the acid side. This nitrate can be for example an alkali nitrate (sodium, potassium), ammonium nitrate, a nitrate of an alkaline earth metal (calcium, magnesium) etc.
For the implementation of this process, one can, for example, operate in the following manner: First decomposes nitrogenous lime with carbonic acid in the presence of water and a cyanamide solution is obtained. free which is filtered to get rid of the carbonate of lime, charcoal and other insoluble im purities.
This operation is repeated with the filtered solution which thus returns to successive extractions, in order to be able to obtain as large a concentration as possible of cyanamide. Considering the instability of the concentrated solutions of this body, especially in the presence of weak bases, care must be taken to avoid prolonged contact of the solutions with nitrogenous lime; it is, on the other hand, necessary to rid the residue completely of all traces of free cyanamide retained by the carbon and carbonate of lime.
To achieve these results without compromising the desired goal, the solutions used for multiple extractions should be monitored, taking care to slightly acidify them by adding small amounts of acid or keeping them away from the environment. 'air, that is to say in an atmosphere of carbon dioxide which will be introduced under pressure if possible.
The concentrated cyanamide solution obtained is added to 53 or <B> 600 </B> B sulfuric acid and a corresponding amount of alkali, ammoniacal, magnesium nitrate, etc.
The mixture is left to stand overnight and the mixture is heated in a water bath until the free cyanamide has completely disappeared, which generally requires one to two hours.
The urea nitrate formed is deposited in the cold in transparent spangled crystals and can optionally be separated from the sulphate of ammonium, potassium, magnesium, etc. by filtration.
The mixture of urea nitrate and ammonium or potassium sulphate can often be used as it is as a fertilizer after having been free of all excess moisture without prior separation.
In view of the fact that the acid which is used for the conversion of cyanamide can be used within certain limits in variable quantities, it is also possible to obtain mixtures containing free urea and urea nitrate, or else urea, urea nitrate and alkali, ammoniacal, magnesian sulphates etc.
Ammonium sulfate in solution, separated by filtration from the urea nitrate crystals, as described above, can be converted back to ammonium nitrate by treating the concentrated solution with nitrate of lime. Lime sulphate precipitates and absorbs two water molecules, turning into plaster. The ammonia nitrate in highly concentrated solution is evaporated to dryness and can be used again. The mixture of lime sulfate and ammonium nitrate obtained as a by-product can also be dried directly and used as it is as a fertilizer in the agi-ictiltui, e.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH98564T | 1921-05-03 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH98564A true CH98564A (en) | 1923-04-16 |
Family
ID=4356406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH98564D CH98564A (en) | 1921-05-03 | 1921-05-03 | Process for the manufacture of a fertilizer based on urea nitrate from cyanamide. |
Country Status (1)
| Country | Link |
|---|---|
| CH (1) | CH98564A (en) |
-
1921
- 1921-05-03 CH CH98564D patent/CH98564A/en unknown
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