IP Library Granted Patent US 9,464,008
Granted Patent B2
US 9,464,008 · App. 13/743,090 · Granted Oct 11, 2016

Process for preparing ammonium sulfate nitrate

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Quick Facts
Patent No.
US 9,464,008
App. No.
13/743,090
Granted
Oct 11, 2016
Kind
B2
Abstract

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.

Claims (30)

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.

Assignments (5)
SECURITY INTEREST Recorded Oct 27, 2021
From: ADVANSIX INC.; ADVANSIX RESINS & CHEMICALS LLC
To: TRUIST BANK, AS ADMINISTRATIVE AGENT
Reel/Frame 057940/0794 →
RELEASE OF SECURITY INTEREST Recorded Oct 27, 2021
From: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
To: ADVANSIX INC.; ADVANSIX RESINS & CHEMICALS LLC
Reel/Frame 057941/0536 →
SECURITY INTEREST Recorded Oct 17, 2016
From: ADVANSIX INC.; ADVANSIX RESINS & CHEMICALS LLC
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 040382/0909 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 13, 2016
From: HONEYWELL INTERNATIONAL INC.
To: ADVANSIX RESINS & CHEMICALS LLC
Reel/Frame 040337/0820 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 30, 2013
From: BARTHE, STEPHANIE C.; KWEEDER, JAMES A.; AZIMOVA, MARIA A.; WISSINGER, RAYMOND G.; PACE, CHRISTOPHER B.; MCGILL, JOSHUA H.; COCHRAN, KEITH D.; HOWES, ANDREW J.
To: HONEYWELL INTERNATIONAL INC.
Reel/Frame 029725/0631 →