IP Library Granted Patent US 10,745,303
Granted Patent B2
US 10,745,303 · App. 15/797,492 · Granted Aug 18, 2020

Process for decontamination of hazardous sulfur compounds in sour water tanks

Inventors: Stephen D. Matza (Sugarland, TX); Jack G. Frost (Duncan, OK)
Assignee: United Laboratories International, LLC
C02F1/725C02F1/02C02F1/38C02F1/68C10G29/04C10G29/20C02F2101/101C02F2103/365C02F2209/02C02F2305/02C07D265/32C09K8/532C09K2208/20C10G2300/207C10G2300/807E21B21/063E21B43/34
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Quick Facts
Patent No.
US 10,745,303
App. No.
15/797,492
Granted
Aug 18, 2020
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 (29)

1. A method for treating contaminants in water, comprising:

(A) contacting the water with a methylmorpholine-N-oxide solution while in a presence, of iron oxide, wherein the contaminants comprise hydrogen sulfide, iron sulfides, or any combinations thereof, wherein the water is in a vessel, wherein the methylmorpholine-N-oxide solution is introduced to the vessel to contact the water, wherein the vessel is a tank, wherein the iron oxide comprises Fe 2 O 3 ·7H 2 O, Fe 2 O 3 ·10H 2 O, or any combination thereof, wherein the methylmorpholine-N-oxide solution is introduced to the vessel by a drum pump, a tank truck, or any combination thereof;

(B) treating the water by allowing a reaction to occur between the methylmorpholine N-oxide and the contaminants in the presence of the iron oxide to produce elemental sulfur and thiosulphate reaction products; and

(C) removing the elemental sulfur and the thiosulphate reaction products from the water by centrifuge.

2. 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.

3. The method of claim 1 , wherein the methylmorpholine-N-oxide solution is not heated before introduction to the vessel.

4. The method of claim 1 , wherein a molar ratio of methylmorpholine-N-oxide to contaminant is about 1.0 mole methylmorpholine-N-oxide:1.0 mole contaminant to about 3.0 moles methylmorpholine-N-oxide:1.0 mole contaminant.

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

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

7. The method of claim 1 , wherein the reaction is irreversible.

8. A method for treating contaminants in water, comprising:

(A) contacting the water with a methylmorpholine-N-oxide solution while in a presence of iron oxide, wherein the contaminants comprise hydrogen sulfide, iron sulfides, or any combinations thereof, wherein the iron oxide is present in the water in an amount from about 100 ppm to about 1,000 ppm iron oxide;

(B) treating the water by allowing the methylmorpholine-N-oxide to react with the contaminants in the presence of the iron oxide to produce elemental sulfur and thiosulfate reaction products, further comprising introducing steam to contact the water, wherein introducing the steam to contact the water increases a temperature of the water; and

(C) removing the elemental sulfa and the thiosulfate reaction products from the water.

9. The method of claim 8 , wherein the methylmorpholine-N-oxide solution comprises between about 1 weight volume % and about 60 weight volume % methylmorpholine-N-oxide.

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

11. The method of claim 8 , wherein the iron oxide comprises ferrous or ferric oxides that are hydrated.

12. The method of claim 8 , wherein the methylmorpholine-N-oxide solution reacts with the contaminants from about one hour to about fifty hours.

13. The method of claim 8 , wherein the methylmorpholine-N-oxide solution is not heated before the contacting step (A).

14. The method of claim 8 , wherein treating the water provides a treated water, and wherein the treated water comprises 0 ppm hydrogen sulfide.

15. The method of claim 8 , wherein the reaction is irreversible.

16. A method for treating contaminants in water, comprising:

(A) contacting the water with a methylmorpholine-N-oxide solution while in a presence of iron oxide, wherein the contaminants comprise hydrogen sulfide, iron sulfides, or any combinations thereof;

(B) treating the water by allowing the methylmorpholine-N-oxide to react with the contaminants in the presence of the iron oxide to produce elemental sulfur and thiosulfate reaction products; and

(C) removing the elemental sulfur and thiosulfate reaction products from the water, further comprising recirculating a mixture of the water and the methylmorpholine-N-oxide solution, wherein the re-circulating comprises re-circulating between about one volume of a total amount of the mixture of the water and the methylmorpholine-N-oxide to about two volumes of the total amount of the mixture the water and the methylmorpholine-N-oxide.

17. The method of claim 16 , wherein the re-circulating further comprises heating the water and the methylmorpholine-N-oxide.

18. The method of claim 17 , wherein the heating comprises a heat exchanger providing heat to the water and the methylmorpholine-N-oxide.

19. The method of claim 17 , wherein heating the water and methylmorpholine-N-oxide solution decreases reaction time.

20. The method of claim 16 , wherein the reaction is irreversible.

Assignments (4)
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 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 13, 2018
From: MATZA, STEPHEN D; FROST, JACK G
To: UNITED LABORATORIES INTERNATIONAL, LLC
Reel/Frame 045187/0148 →
Continuity (4)
Continuation 14512987 · Oct 13, 2014
Continuation 13650561 · Oct 12, 2012
Provisional Application 61546481 · Oct 12, 2011
Related Publication 20180297874A1 · Oct 18, 2018
Cited By (2)
US 12,187,631 US 12,503,657