IP Library Granted Patent US 11,267,705
Granted Patent B2
US 11,267,705 · App. 16/319,610 · Granted Mar 8, 2022

Process for reducing the hydrogen sulphide content in non-gaseous sulphur compositions using a zinc-based scavenger

Inventors: Helen Jayne Davies (Frodsham, GB); Dawid John D'Melo (Karnataka, IN); Reginald Lambert (Alberta, CA)
Assignee: SHELL OIL COMPANY
C01B17/0232C01B17/0243C01G9/00
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Quick Facts
Patent No.
US 11,267,705
App. No.
16/319,610
Granted
Mar 8, 2022
Kind
B2
Abstract

A process for reducing the hydrogen sulphide content in a composition containing or consisting of hydrogen sulphide and non-gaseous elemental sulphur, comprising contacting the composition with a scavenger, wherein the scavenger is chosen from the group consisting of zinc oxide, zinc carbonate, zinc hydroxy carbonate or a combination of two or more of these.

Claims (19)

1. A process for reducing the hydrogen sulphide content in a composition containing hydrogen sulphide and non-gaseous elemental sulphur, comprising contacting the composition with a scavenger, wherein the scavenger is chosen from the group consisting of zinc oxide, zinc carbonate, zinc hydroxy carbonate or a combination of two or more of these.

2. The process including the step of contacting a composition containing or consisting of hydrogen sulphide and non-gaseous elemental sulphur with one or more scavenger(s), wherein the composition contains more than 10 ppmw and less than 10000 ppmw hydrogen sulphide based on the total weight of the composition, and wherein the one or more scavenger(s) are chosen from the group consisting of zinc carbonate, zinc hydroxy carbonate and mixtures thereof.

3. The process according to claim 1 , wherein the composition containing or consisting of hydrogen sulphide and non-gaseous elemental sulphur is a composition containing or consisting of hydrogen sulphide and liquid elemental sulphur.

4. The process according to claim 3 , wherein the composition contains between equal to or more than 99.000 wt. % and equal to or less than 99.999 wt. % of liquid elemental sulphur and between equal to or more than 10 ppmw and equal to or less than 10000 ppmw of hydrogen sulphide, based on the total weight of the composition.

5. The process according to claim 1 , wherein the scavenger is a zinc hydroxy carbonate.

6. The process according to claim 1 , wherein the scavenger is contacted with the composition in an amount of equal to or more than 0.005 wt. % and equal to or less than 0.5 wt. % scavenger based on the total weight of the composition.

7. The process according to claim 1 , wherein the weight ratio of the scavenger to hydrogen sulphide is equal to or more than 0.01 to 1 (0.01:1) and equal to or less than 100 to 1 (100:1).

8. The process according to claim 1 , wherein the process comprises:

a step comprising mixing the scavenger and a composition containing hydrogen sulphide and solid elemental sulphur to form a mixture containing hydrogen sulphide, solid elemental sulphur and scavenger;

a subsequent step comprising melting the mixture containing hydrogen sulphide, solid elemental sulphur and scavenger to form a mixture containing hydrogen sulphide, liquid elemental sulphur and scavenger.

9. The process according to claim 1 , wherein the process comprises:

a step comprising melting a composition containing hydrogen sulphide and solid elemental sulphur to form a composition containing hydrogen sulphide and liquid elemental sulphur; and

a subsequent step comprising mixing the scavenger and the composition containing hydrogen sulphide and liquid elemental sulphur to form a mixture containing hydrogen sulphide, liquid elemental sulphur and scavenger.

10. The process according to claim 1 , wherein the scavenger is deposited on a solid carrier.

11. The process according to claim 1 , wherein the composition containing or consisting of hydrogen sulphide and non-gaseous elemental sulphur is added to the scavenger and the composition and scavenger are mixed.

12. The process according to claim 1 , wherein the process is a batch-wise or semi-batchwise process and the scavenger is mixed with the composition by means of the agitation associated with transport from a first location to a second location.

13. The process according to claim 1 , thereby forming a product composition.

14. The process according to claim 13 , wherein the product composition is directly or indirectly at least partly solidified into solid elemental sulphur.

15. The mixture comprising non-gaseous elemental sulphur and zinc hydroxy carbonate.

Assignments (2)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 27, 2022
From: DAVIES, HELEN JAYNE; D'MELO, DAWID JOHN; LAMBERT, REGINALD
To: SHELL OIL COMPANY
Reel/Frame 058790/0985 →