Fertilizer compositions and methods of making and using the same
US-9527779-B2 · Dec 27, 2016 · US
US9464008B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9464008-B2 |
| Application number | US-201313743090-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 16, 2013 |
| Priority date | Feb 1, 2012 |
| Publication date | Oct 11, 2016 |
| Grant date | Oct 11, 2016 |
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Ammonium sulfate nitrate double salts may be produced using a process that result in complete or nearly complete conversion to the 2:1 double salt. In some embodiments, the disclosure pertains to methods of controlling moisture content during the production process.
Opening claim text (preview).
We claim: 1. A method of producing a solid ammonium sulfate nitrate composition comprising the step of: solidifying a melt slurry including ammonium sulfate and ammonium nitrate in a granulation bed to form the solid ammonium sulfate nitrate composition comprising ammonium sulfate nitrate 2:1 double salt, wherein the melt slurry has a molar ratio of ammonium sulfate to ammonium nitrate of about 0.9:1 to about 1.1:1, wherein the granulation bed has an operating temperature of 90° C. to 120° C. and the solid ammonium sulfate nitrate composition has a moisture content of between 0.4 wt. % and 2.0 wt. % wherein the solid ammonium sulfate nitrate composition is primarily in the form of the ammonium sulfate nitrate 2:1 double salt and includes less than about 7 wt. % of unreacted ammonium nitrate and ammonium sulfate nitrate 3:1 double salt. 2. The method of claim 1 , wherein the granulation bed has an operating temperature of 90° C. to 105° C. 3. The method of claim 1 , wherein said solidifying step further comprises adding steam to the granulation bed. 4. The method of claim 1 , wherein said solidifying step further comprises spraying an aqueous solution onto the granulation bed. 5. The method of claim 1 , wherein said solidifying step further comprises selectively modifying a rate of air flow through the granulation bed. 6. The method of claim 1 , wherein said solidifying step further comprises: adding steam to the granulation bed; and selectively modifying a rate of air flow through the granulation bed. 7. A method of producing a solid ammonium sulfate nitrate composition including ammonium sulfate nitrate 2:1 double salt, said method comprising the steps of: adding a melt slurry including ammonium sulfate and ammonium nitrate to a granulation device, wherein the melt slurry has a molar ratio of ammonium sulfate to ammonium nitrate of about 0.9:1 to about 1.1:1; adding an amount of supplemental ammonia to the granulation device in addition to ammonia provided in the melt slurry; solidifying the melt slurry in the granulation device in the presence of the supplemental ammonia to form a solid granule mixture including ammonium sulfate nitrate 2:1 double salt, wherein the solid ammonium sulfate nitrate composition is primarily in the form of the ammonium sulfate nitrate 2:1 double salt and includes less than about 7 wt. % of unreacted ammonium nitrate and ammonium sulfate nitrate 3:1 double salt. 8. The method of claim 7 , wherein said adding steps further comprise, respectively: adding the melt slurry to a material bed of the granulation device; and adding the supplemental ammonia to the material bed of the granulation device. 9. The method of claim 7 , wherein the solidification device is a granulation device, and said adding step further comprises: adding the supplemental ammonia to a material bed of a drying device downstream of the granulation device. 10. A method of producing a solid ammonium sulfate nitrate composition, said method comprising the steps of: adding a melt slurry including ammonium sulfate and ammonium nitrate to a granulation bed of a granulation device wherein the melt slurry has a molar ratio of ammonium sulfate to ammonium nitrate of about 0.9:1 to about 1.1:1; solidifying the melt slurry in the granulation bed of the granulation device to form the solid ammonium sulfate nitrate composition, including ammonium sulfate nitrate 2:1 double salt; drying the solid mixture in a drying device such that a moisture content of the solid ammonium sulfate nitrate composition in the drying device is between 0.4 wt. % and 1.5 wt. %, wherein the solid ammonium sulfate nitrate composition is primarily in the form of the ammonium sulfate nitrate 2:1 double salt and include less than about 7 wt. % of unreacted ammonium nitrate and ammonium sulfate nitrate 3:1 double salt. 11. The method of claim 10 , wherein said controlling step further comprises selectively modifying a rate of air flow through the drying device. 12. A method of producing a solid ammonium sulfate nitrate composition including ammonium sulfate nitrate 2:1 double salt, said method comprising the steps of: solidifying a melt slurry including ammonium sulfate and ammonium nitrate in a granulation device to form solid ammonium sulfate nitrate granules including ammonium sulfate nitrate 2:1 double salt, wherein the melt slurry has a molar ratio of ammonium sulfate to ammonium nitrate of about 0.9:1 to about 1.1:1, wherein the solid ammonium sulfate nitrate has a moisture content of 0.4 to 2.0 wt. %, wherein the solid ammonium sulfate nitrate granules include less than about 7 wt. % of unreacted ammonium nitrate and ammonium sulfate nitrate 3:1 double salt. 13. The method of claim 12 , wherein the solid ammonium sulfate nitrate has a moisture content between 0.5 and 1.5 wt. %. 14. The method of claim 1 , wherein the solid ammonium sulfate nitrate composition includes less than about 3 wt. % of ammonium nitrate and ammonium sulfate nitrate 3:1 double salt. 15. The method of claim 12 , wherein the solid ammonium sulfate nitrate granules include less than about 3 wt. % of unreacted ammonium nitrate and ammonium sulfate nitrate 3:1 double salt. 16. The method of claim 1 , wherein the granulation bed has an operating temperature of 90° C. to 105° C., the solid ammonium sulfate nitrate composition has a moisture content between 0.5 wt. % and 2.0 wt. %, and the solid ammonium sulfate nitrate composition includes less than about 3 wt. % of unreacted ammonium nitrate and ammonium sulfate nitrate double salt. 17. The method of claim 7 , wherein the amount of supplemental ammonium is sufficient to raise a pH of the solid ammonium sulfate nitrate composition exiting the granulation bed to a pH of about 5.2.
Fertilisers containing other salts of ammonia or ammonia itself, e.g. gas liquor · CPC title
Ammonium nitrate fertilisers · CPC title
Granulation (apparatus B01J2/00); Pelletisation; Stabilisation; Colouring · CPC title
Preventing coalescing or controlling form or size of the crystals · CPC title
Post-treatment · CPC title
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