IP Library Granted Patent US 8,702,994
Granted Patent B2
US 8,702,994 · App. 12/415,283 · Granted Apr 22, 2014

Sodium nitrite oxidation of hydrogen sulfide

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Quick Facts
Patent No.
US 8,702,994
App. No.
12/415,283
Granted
Apr 22, 2014
Kind
B2
Abstract

A method for treating hydrogen sulfide in a solution includes providing the solution containing hydrogen sulfide. The method also includes adding sodium nitrite to the solution in an amount suitable to react with the hydrogen sulfide and treat the hydrogen sulfide.

Claims (16)

1. A method for removing hydrogen sulfide from water, wherein the water comprises hydrogen sulfide, comprising:

adding sodium nitrite to the water in an amount suitable to react with the hydrogen sulfide in the water and remove hydrogen sulfide from the water; and

adding a pH buffer periodically to the water to maintain the pH of the water between about 7.0 to about 9.0 and to remove free ammonia from the water.

2. The method of claim 1 , wherein the water comprises from about 2,000 mg/liter to about 25,000 mg/liter hydrogen sulfide.

3. The method of claim 1 , wherein the water comprises from about 5,000 mg/liter to about 25,000 mg/liter hydrogen sulfide.

4. The method of claim 1 , wherein the water comprises from about 10,000 mg/liter to about 25,000 mg/liter hydrogen sulfide.

5. The method of claim 1 , wherein the sodium nitrite is added at a weight ratio to hydrogen sulfide from about 0.676:1 to about 5.0:1.

6. The method of claim 1 , wherein the sodium nitrite is added at a weight ratio to hydrogen sulfide from about 0.676:1 to about 1.353:1.

7. The method of claim 1 , wherein the pH buffer comprises an acidic buffering chemical.

8. The method of claim 1 , wherein the pH buffer comprises citric acid, phosphoric acid, boric acid, or any combinations thereof.

9. The method of claim 1 , wherein the pH buffer comprises citric acid, phosphoric acid, or any combinations thereof.

10. The method of claim 1 , wherein the pH buffer comprises phosphoric acid.

11. The method of claim 1 , wherein the reaction between the sodium nitrite and the hydrogen sulfide is carried out at between about 40° C. and about 70° C.

12. The method of claim 1 , wherein the reaction between the sodium nitrite and the hydrogen sulfide is carried out at between about 40° C. and about 50° C.

13. The method of claim 1 , wherein the reaction between the sodium nitrite and the hydrogen sulfide produces ammonia, the method further comprises blowing an ammonia-removal gas to remove the produced ammonia.

14. The method of claim 13 , wherein the ammonia-removal gas is blown by a compressor.

Assignments (7)
MERGER Recorded Mar 15, 2025
From: CR3 ZYMEFLOW, INC.
To: ZYMEFLOW, INC.
Reel/Frame 070523/0169 →
MERGER Recorded Mar 13, 2025
From: TRISTAR GLOBAL ENERGY SOLUTIONS, INC.
To: CR3 ZYMEFLOW, INC.
Reel/Frame 070508/0396 →
MERGER Recorded Mar 12, 2025
From: UNITED LABORATORIES INTERNATIONAL, LLC
To: TRISTAR GLOBAL ENERGY SOLUTIONS, INC.
Reel/Frame 070491/0243 →
RELEASE OF SECURITY INTEREST Recorded Sep 8, 2023
From: ABACUS FINANCE GROUP LLC
To: UNITED LABORATORIES INTERNATIONAL LLC
Reel/Frame 064839/0568 →
SECURITY INTEREST Recorded Jan 5, 2015
From: UNITED LABORATORIES INTERNATIONAL, LLC; GLOBAL VAPOR CONTROL, INC.
To: ABACUS FINANCE GROUP, LLC, AS AGENT
Reel/Frame 034631/0429 →
RELEASE OF SECURITY INTEREST Recorded Jan 5, 2015
From: TEXAS CAPITAL BANK, NATIONAL ASSOCIATION
To: UNITED LABORATORIES INTERNATIONAL, LLC
Reel/Frame 034634/0719 →
SECURITY AGREEMENT Recorded Oct 2, 2013
From: UNITED LABORATORIES INTERNATIONAL, LLC
To: TEXAS CAPITAL BANK, NATIONAL ASSOCIATION
Reel/Frame 031327/0650 →