IP Library Granted Patent US 12,187,609
Granted Patent B2
US 12,187,609 · App. 17/585,990 · Granted Jan 7, 2025

Purification of bis(fluorosulfonyl) imide

Inventors: Matthew H. Luly (Hamburg, NY); Bernard E. Pointner (Buffalo, NY)
Assignee: Honeywell International Inc.
C01B21/093
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Quick Facts
Patent No.
US 12,187,609
App. No.
17/585,990
Granted
Jan 7, 2025
Kind
B2
Abstract

A method of producing purified bis(fluorosulfonyl) imide includes providing a liquid mixture including bis(fluorosulfonyl) imide and fluorosulfonic acid and then contacting the liquid mixture with gaseous ammonia. The gaseous ammonia reacts with the fluorosulfonic acid to produce ammonium fluorosulfate. The method further includes separating the liquid mixture from the ammonium fluorosulfate.

Claims (26)

1. A method of producing purified bis(fluorosulfonyl) imide, the method comprising:

reacting urea with fluorosulfonic acid to form a first liquid mixture comprising bis(fluorosulfonyl) imide and unreacted fluorosulfonic acid;

contacting the first liquid mixture with gaseous ammonia, wherein the gaseous ammonia reacts with the fluorosulfonic acid to produce a second liquid mixture comprising ammonium fluorosulfate; and

separating the ammonium fluorosulfate from the second liquid mixture.

2. The method of claim 1 , wherein after the reacting step, a concentration of the fluorosulfonic acid in the first liquid mixture is from about 0.001 mol % to about 70 mol %.

3. The method of claim 1 , wherein contacting the first liquid mixture with gaseous ammonia includes introducing the gaseous ammonia into a headspace of a vessel containing the first liquid mixture.

4. The method of claim 3 , wherein the gaseous ammonia is supplied at a pressure between about 100 kPa and about 200 kPa.

5. The method of claim 1 , wherein contacting the first liquid mixture with gaseous ammonia includes bubbling the gaseous ammonia into the first liquid mixture.

6. The method of claim 1 , wherein contacting the first liquid mixture with gaseous ammonia includes flowing the gaseous ammonia and the first liquid mixture in a counterflow column.

7. The method of claim 1 , wherein separating the the ammonium fluorosulfate from the second liquid mixture includes filtering the ammonium fluorosulfate from the second liquid mixture.

8. The method of claim 1 , wherein separating the ammonium fluorosulfate from the second liquid mixture includes flash distilling the bis(fluorosulfonyl) imide from the ammonium fluorosulfate.

9. The method of claim 1 , wherein a concentration of the bis(fluorosulfonyl) imide in a remaining second liquid mixture obtained after separating the ammonium fluorosulfate from the second liquid mixture is from about 90 mol % to about 99.95 mol %.

10. The method of claim 1 , further comprising:

providing a remaining second liquid mixture obtained after separating the ammonium fluorosulfate from the second liquid mixture, the remaining second liquid mixture including the bis(fluorosulfonyl) imide and residual fluorosulfonic acid;

contacting the remaining second liquid mixture with gaseous ammonia, wherein the gaseous ammonia reacts with the residual fluorosulfonic acid in the remaining second liquid mixture to produce a third liquid mixture comprising additional ammonium fluorosulfate; and

separating the additional ammonium fluorosulfate from the third liquid mixture.

11. The method of claim 10 , wherein in the providing step, the concentration of the residual fluorosulfonic acid in the remaining second liquid mixture is from about 0.1 mol % to about 20 mol %.

12. The method of claim 10 , wherein contacting the remaining second liquid mixture with gaseous ammonia includes introducing the gaseous ammonia into a headspace of a vessel containing the remaining second liquid mixture.

13. The method of claim 12 , wherein the gaseous ammonia is supplied at a pressure between about 100 kPa and about 200 kPa.

14. The method of claim 10 , wherein contacting the remaining second liquid mixture with gaseous ammonia includes bubbling the gaseous ammonia into the remaining second liquid mixture.

15. The method of claim 10 , wherein contacting the remaining second liquid mixture with gaseous ammonia includes flowing the gaseous ammonia and the remaining second liquid mixture in a counterflow column.

16. The method of claim 10 , wherein separating the additional ammonium fluorosulfate from the third liquid mixture includes filtering the ammonium fluorosulfate from the third liquid mixture.

17. The method of claim 10 , wherein separating the additional ammonium fluorosulfate from the third liquid mixture includes flash distilling the bis(fluorosulfonyl) imide from the ammonium fluorosulfate.

18. The method of claim 10 , wherein the bis(fluorosulfonyl) imide concentration in a remaining third liquid mixture obtained after separating the additional ammonium fluorosulfate from the third liquid mixture is from about 98 mol % to about 99.95 mol %.

19. The method of claim 1 , further including distilling the remaining second liquid mixture including the bis(fluorosulfonyl) imide and the residual fluorosulfonic acid before the providing step.

20. The method of claim 19 , wherein in the providing step, a concentration of the fluorosulfonic acid in the remaining second liquid mixture is from about 1 mol % to about 20 mol %.

Assignments (2)
SECURITY INTEREST Recorded Jan 12, 2026
From: SOLSTICE ADVANCED MATERIALS US, INC.
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 074569/0260 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 11, 2025
From: LULY, MATTHEW H.; POINTNER, BERNARD E.
To: HONEYWELL INTERNATIONAL INC.
Reel/Frame 070481/0306 →
Continuity (3)
Continuation 16842646 · Apr 7, 2020
Provisional Application 62834815 · Apr 16, 2019
Related Publication 20220144638A1 · May 12, 2022
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