IP Library Granted Patent US 9,512,019
Granted Patent B2
US 9,512,019 · App. 13/650,561 · Granted Dec 6, 2016

Process for decontamination of hazardous sulfur compounds in sour water tanks

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Quick Facts
Patent No.
US 9,512,019
App. No.
13/650,561
Granted
Dec 6, 2016
Kind
B2
Abstract

A method and system treat contaminated water. In one embodiment, the method comprises treating contaminated water by introducing a methylmorpholine-N-oxide solution to a vessel. The vessel contains the contaminated water and iron oxide. The contaminated water comprises contaminants. In addition, the methylmorpholine-N-oxide solution comprises methylmorpholine-N-oxide and water. The method further comprises contacting the methylmorpholine-N-oxide solution with the contaminated water. In addition, the method comprises treating the contaminated water by allowing the methylmorpholine-N-oxide to react with the contaminants in the presence of the iron oxide.

Claims (23)

1. A method for treating contaminated water, comprising:

(A) introducing a methylmorpholine-N-oxide solution to a vessel, wherein the vessel contains the contaminated water and iron oxide, and wherein the contaminated water comprises contaminants, and wherein the methylmorpholine-N-oxide solution comprises methylmorpholine-N-oxide and water;

(B) contacting the methylmorpholine-N-oxide solution with the contaminated water; and

(C) treating the contaminated water by allowing the methylmorpholine-N-oxide to react with the contaminants in the presence of the iron oxide.

2. The method of claim 1 , wherein the contaminants comprise hydrogen sulfide, iron sulfides, or any combinations thereof.

3. The method of claim 2 , wherein the contaminants comprise hydrogen sulfide.

4. The method of claim 3 , wherein treating the contaminated water comprises converting the hydrogen sulfide to elemental sulfur.

5. The method of claim 4 , wherein the elemental sulfur is removed from the vessel.

6. The method of claim 1 , wherein the methylmorpholine-N-oxide solution comprises between about 1 weight volume % and about 60 weight volume % methylmorpholine-N-oxide.

7. The method of claim 1 , wherein the methylmorpholine-N-oxide solution is introduced to the vessel in an amount to provide a mole ratio of methylmorpholine-N-oxide to contaminant in the vessel from about 1.0 mole methylmorpholine-N-oxide: 1.0 mole contaminant to about 3.0 moles methylmorpholine-N-oxide: 1.0 mole contaminant.

8. The method of claim 1 , further comprising introducing steam to the contaminated water.

9. The method of claim 8 , wherein the steam comprises 150 psig steam or less.

10. The method of claim 8 , further comprising introducing the steam to the vessel to increase the temperature of the contaminated water to a temperature from about 75° F. to about 212° F.

11. The method of claim 1 , wherein the iron oxide comprises ferrous or ferric oxides that are hydrated.

12. The method of claim 1 , wherein the iron oxide comprises Fe 2 O 3 .7H 2 O, Fe 2 O 3 .10H 2 O, or any combinations thereof.

13. The method of claim 1 , wherein the vessel comprises from about 100 ppm iron oxide to about 1,000 ppm iron oxide.

14. The method of claim 1 , wherein the methylmorpholine-N-oxide reacts with the contaminants from about one hour to about fifty hours.

15. The method of claim 1 , wherein treating the contaminated water provides a treated water, and wherein the treated water comprises about 0 ppm hydrogen sulfide.

16. The method of claim 1 , wherein treating the contaminated water provides a treated water, wherein the treated water is removed from the vessel.

17. The method of claim 1 , further comprising recirculating the contaminated water and the methylmorpholine-N-oxide solution.

18. The method of claim 17 , wherein recirculating comprises recirculating between about one volume of the total amount of contaminated water and methylmorpholine-N-oxide solution in the vessel to about two volumes of the total amount of contaminated water and methylmorpholine-N-oxide solution in the vessel.

19. The method of claim 18 , wherein recirculating further comprises heating the contaminated water and methylmorpholine-N-oxide solution.

20. The method of claim 19 , wherein the heating comprises a heat exchanger providing heat to the contaminated water and methylmorpholine-N-oxide solution.

Assignments (8)
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 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 17, 2014
From: MATZA, STEPHEN D.; FROST, JACK G.
To: UNITED LABORATORIES INTERNATIONAL, LLC
Reel/Frame 032703/0063 →
SECURITY AGREEMENT Recorded Oct 2, 2013
From: UNITED LABORATORIES INTERNATIONAL, LLC
To: TEXAS CAPITAL BANK, NATIONAL ASSOCIATION
Reel/Frame 031327/0650 →