US1810858A - Processes for the decomposition of crude phosphate - Google Patents
Processes for the decomposition of crude phosphate Download PDFInfo
- Publication number
- US1810858A US1810858A US406504A US40650429A US1810858A US 1810858 A US1810858 A US 1810858A US 406504 A US406504 A US 406504A US 40650429 A US40650429 A US 40650429A US 1810858 A US1810858 A US 1810858A
- Authority
- US
- United States
- Prior art keywords
- decomposition
- crude phosphate
- acid
- processes
- potash
- 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 - Lifetime
Links
- 238000000034 method Methods 0.000 title description 9
- 238000000354 decomposition reaction Methods 0.000 title description 8
- 229910019142 PO4 Inorganic materials 0.000 title description 7
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 title description 6
- 239000010452 phosphate Substances 0.000 title description 6
- 229910001868 water Inorganic materials 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 9
- 229940072033 potash Drugs 0.000 description 9
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 9
- 235000015320 potassium carbonate Nutrition 0.000 description 9
- 239000010440 gypsum Substances 0.000 description 8
- 229910052602 gypsum Inorganic materials 0.000 description 8
- 238000005406 washing Methods 0.000 description 8
- 239000002253 acid Substances 0.000 description 7
- 235000021317 phosphate Nutrition 0.000 description 6
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 4
- 229910052939 potassium sulfate Inorganic materials 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 239000001120 potassium sulphate Substances 0.000 description 3
- 235000011151 potassium sulphates Nutrition 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- NYRAVIYBIHCEGB-UHFFFAOYSA-N [K].[Ca] Chemical compound [K].[Ca] NYRAVIYBIHCEGB-UHFFFAOYSA-N 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B11/00—Fertilisers produced by wet-treating or leaching raw materials either with acids in such amounts and concentrations as to yield solutions followed by neutralisation, or with alkaline lyes
- C05B11/04—Fertilisers produced by wet-treating or leaching raw materials either with acids in such amounts and concentrations as to yield solutions followed by neutralisation, or with alkaline lyes using mineral acid
Definitions
- the composition of may be varied within somewhat wide or pentasulphate (K SO 502180 H 0),
- the invention consists in effecting the washing of the potash fromthese double com ounds in presence of some free acid.
- pentasulphate is treated at e. g. with ammonia or potash, to
- the process is carried out in such a manner that the washing of the gypsum slime containin the potassium-calcium double salts is efiected in two stages with an intermediate agitation with a dilute water solution of the particular acid being used.
- the gypsum sllme is washed with a part of the quantity of washing water as usual; it is then agitated. with water containing acid and is finally completely washed out with water.
- the acid from the stirring lye together with the last washing water is employed, as usual, for the decomposition of fresh crude phosphate.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
Patented June 16, 1931 UNITED STATES PATENT, OFFICE THEODOR 'rrroRssELI. AND AUGUST xnIsrENssoN, or GASSEL, GERMANY PROCESSES FOR THE DECOMPOSITION OF CRUDE PHOSPHATE No Drawing. Application filed November 11, 1929, SerialNo. 406,504, and in Germany November 28, 1928.
It is already known to use a mixture of potassium sulphate and an acid for the decomposition of crude phosphates in place of sulphuric acid. This method of working is 6 rational, since the value of the potassium sulphate lies exclusively in the potash and the sulphuric acid is therefore introduced into the process without cost. If nitric acid is used, gypsum and a solution of po- 1 tassium nitrate and phosphoric acid or a potassium vphospate or a mixture of both are obtained; it is also possible, by evaporating this solution after previous neutralization, make a which limits.
It has now been proved by experiments that owing to excessive losses of potash this process "cannot be carried out forthwith. The whole economy of the process may be ruined becaus the potash, as stated above, is the valuable constitutent of potassium sulhate.
This loss in potash arises because not only gypsum is formed in the decomposition but also, according to the concentration and the temperaturasyngenite (K SO CaSO ,H O)
mixed fertilizer, the composition of may be varied within somewhat wide or pentasulphate (K SO 502180 H 0),
60 If, or instance,
which precipitate out together with the gypsum and are lost with it (cf. Gmelin-Kraut Handbuch der Anorganischen Chemie, 7th edn., Vol. II, Part I, p. 139).
These double salts are decomposed by water (of. J. H. vant Hofi, Untersuchungen iiber die Bildungsverhaltnisse der Ozeanischen Salzablagerungen, Insbesondere des Stassfurter Salzlagers, pp. 290, 291). By washing with watertherefore the potash could be recovered from the gypsum slime, butquantities of heat are then necessary which are so large that the lye obtained is diluted to such an extent that working in this manner is practically impossible.
The invention consists in effecting the washing of the potash fromthese double com ounds in presence of some free acid. pentasulphate is treated at e. g. with ammonia or potash, to
20 C. with acidified water, improved results are obtained with 100 g. H20+2.7 g. HNOS are dissolved 5.8 g. K2804 with 100 g. H2O+6.1 g. HNO are dissolved 9.5 g K2SO4 whereas accordingto vant Hofl only 3.58 g. K 80 are dissolved in 100 g. H O at 31.8 C.
The process is carried out in such a manner that the washing of the gypsum slime containin the potassium-calcium double salts is efiected in two stages with an intermediate agitation with a dilute water solution of the particular acid being used. First of all, therefore, the gypsum sllme is washed with a part of the quantity of washing water as usual; it is then agitated. with water containing acid and is finally completely washed out with water.
The acid from the stirring lye together with the last washing water is employed, as usual, for the decomposition of fresh crude phosphate.
Having now particularly described and ascertained the nature of our said invention and in what manner the same is to be performed, we declare that what we claim is l.-In a process for the decomposition of crude phosphate with an acid and potassium sulphate with precipitation of gypsum containing double potassium-calcium salts, the recovery of the potash from the said double salts, comprising the steps of washing with water the gypsum containing the said double salts, agitating with water, containing nitric acid, and washing again with water, as set forth.
2. In a process for the decomposition of crude phosphate with recovery'of the potash, as claimed in claim 1, the use of the acid washing liquor obtained in the second step of the recovery in the decomposition of fresh crude phosphate, as set forth.
In testimony tures.
THEODOR THQRSSELL. AUGUST KRISTENSSON.
whereof we afiix our signa-
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE1810858X | 1928-11-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1810858A true US1810858A (en) | 1931-06-16 |
Family
ID=7744287
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US406504A Expired - Lifetime US1810858A (en) | 1928-11-28 | 1929-11-11 | Processes for the decomposition of crude phosphate |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1810858A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2700605A (en) * | 1951-11-10 | 1955-01-25 | Best Fertilizers Co | Process for making a fluid phosphate fertilizer slurry suitable for pelletizing |
| US2739038A (en) * | 1951-08-16 | 1956-03-20 | Henkel & Cie Gmbh | Water soluble ortho phosphates |
-
1929
- 1929-11-11 US US406504A patent/US1810858A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2739038A (en) * | 1951-08-16 | 1956-03-20 | Henkel & Cie Gmbh | Water soluble ortho phosphates |
| US2700605A (en) * | 1951-11-10 | 1955-01-25 | Best Fertilizers Co | Process for making a fluid phosphate fertilizer slurry suitable for pelletizing |
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