Reactor, a structure packing, and a method for improving oxidation of hydrogen sulfide or polysulfides in liquid sulfur

1. A reactor, comprising:

a first inlet for a first stream including liquid sulfur containing polysulfides and dissolved hydrogen sulfide;

a second inlet for a second stream of oxygen-containing gas;

a structured packing comprising corrugated sheeting having elongated cross-flow channels between adjacent sheets, and the structured packing further having side walls in contact with a catalyst;

wherein the amount of catalyst is sufficient to increase the rate of decomposition of the polysulfides and oxidation of the polysulfides and hydrogen sulfide present in the liquid sulfur of the first stream with the second stream; and

wherein the second inlet includes apertures corresponding in size to a flow opening in the structured packing such that bubbles emanating from the apertures have a size that is equal or smaller than a size of the flow opening.

2. The reactor of claim 1 , wherein the structured packing is positioned between the first inlet and the second inlet.

3. The reactor of claim 1 , wherein flow of the first stream through the first inlet is controlled to provide a preselected residence time in the reactor, to achieve a desired level of polysulfides removal from the first stream, and to achieve a desired level of hydrogen sulfide gas removal from the first stream.

4. The reactor of claim 1 , wherein the corrugated sheeting is coated with the catalyst.

5. The reactor of claim 1 , wherein the corrugated sheeting comprises the catalyst.

6. The reactor of claim 1 , wherein the corrugated sheeting secures the catalyst.

7. The reactor of claim 1 , wherein the catalyst is selected from the group consisting of bauxite, titania, alumina, a mixture of silica with thermally stable alumina, a mixture of silica, and titania, and combinations thereof.

8. The reactor of claim 7 , wherein the catalyst is promoted with iron oxide or alkaline metal oxide.

9. The reactor of claim 1 , wherein the corrugation angles vary in a range from 45 degrees to 60 degrees, inclusive.

10. The reactor of claim 1 , wherein the corrugated sheeting includes a plurality of sheets the adjacent sheets are stacked to provide a 2 mm to 12 mm cross-flow channel opening, inclusive, for the first and second streams.

11. The reactor of claim 10 , further comprising a diffuser that includes the apertures.

12. A structured packing for contacting a first stream and a second stream in a reactor, the structured packing comprising:

a catalyst in contact with side walls of a layered sheeting comprising a plurality of corrugated sheets, the corrugations in each sheeting having corrugation angles between 45° and 60°, inclusive, the sheets layered and the corrugation angles varied in a manner that results in non-rectangular tubular cross-flow channels between adjacent sheets that are lossy between adjacent folds of juxtaposed sheets;

wherein the catalyst is a polysulfide and hydrogen sulfide decomposition and oxidation catalyst that is effective to produce SO 2 and elemental sulfur from polysulfide and hydrogen sulfide,

wherein the first stream includes liquid sulfur containing polysulfides and dissolved hydrogen sulfide, and

wherein the second stream includes an oxygen-containing gas.

13. The structured packing of claim 12 , wherein the structured packing is coated with the catalyst.

14. The structured packing of claim 12 , wherein the structured packing is made up of the catalyst.

15. The structured packing of claim 12 , wherein the structured packing secures the catalyst.

16. The structured packing of claim 12 , wherein the catalyst is selected from the group consisting of bauxite, titania, alumina, a mixture of silica with thermally stable alumina, a mixture of silica and titania, and combinations thereof, and wherein the catalyst is positioned in the packing such as to enable reduction of combined polysulfides and hydrogen sulfide to a level of less than 5 ppmv.

17. The structured packing of claim 16 , wherein the catalyst is promoted with iron oxide or alkaline metal oxide.

18. The reactor of claim 12 , wherein the adjacent sheets are layered to provide a 2 mm to 12 mm cross-flow channel opening, inclusive, for the first and second streams.

19. A reactor, comprising:

a first inlet for a first stream including liquid sulfur containing polysulfides and dissolved hydrogen sulfide;

a second inlet for a second stream of oxygen-containing gas; and

a structured packing comprising corrugated sheeting for facilitating contact between the first stream and the second stream, the structured packing further comprising a catalyst;

wherein the amount of catalyst is sufficient to increase the rate of decomposition of the polysulfides and oxidation of the polysulfides and hydrogen sulfide present in the liquid sulfur of the first stream with the second stream; and

wherein the structured packing is positioned between the first inlet and the second inlet, and the second inlet includes apertures corresponding in size to flow openings in the structured packing.

20. A reactor, comprising:

a first inlet for a first stream including liquid sulfur containing polysulfides and dissolved hydrogen sulfide;

a second inlet for a second stream of oxygen-containing gas; and

a structured packing comprising corrugated sheeting for facilitating contact between the first stream and the second stream, the structured packing further comprising a catalyst;

wherein the amount of catalyst is sufficient to increase the rate of decomposition of the polysulfides and oxidation of the polysulfides and hydrogen sulfide present in the liquid sulfur of the first stream with the second stream; and

wherein the corrugated sheeting includes a plurality of sheets stacked to provide a 2 mm to 12 mm cross-flow channel opening, inclusive, for the first and second streams, and a diffuser that releases gas from the second stream in bubbles smaller than the cross-flow channel opening.

21. A method of treating hydrogen sulfide and polysulfides in liquid sulfur, the method comprising:

providing through a first inlet a first stream including liquid sulfur containing polysulfides and hydrogen sulfide; providing through a second inlet a second stream of oxygen-containing gas; and

in a structured packing, contacting the first stream and the second stream, the structured packing having corrugated sheeting with side walls that contact a catalyst, and elongated cross-flow channels at corrugation folds between adjacent sheets;

wherein the catalyst is sufficient to increase the rate of decomposition of polysulfides and oxidation of polysulfides and hydrogen sulfide in the liquid sulfur of the first stream with the second stream; and

wherein the second inlet includes apertures corresponding in size to a flow opening in the structured packing such that hubbies emanating from the apertures have a size that is equal or smaller than a size of the flow opening.

22. The method of claim 21 , further comprising adjusting flow of the first stream through the first inlet to provide a preselected residence time in the reactor, to achieve a desired level of polysulfides removal from the first stream, and to achieve a desired level of hydrogen sulfide gas removal from the first stream.

23. The method of claim 21 , wherein the side walls are coated with the catalyst.

24. The method of claim 21 , wherein the structured packing comprises the catalyst.

25. The method of claim 21 , wherein the structured packing secures the catalyst.

26. The method of claim 21 wherein the second stream contacts a distributor.

27. The method of claim 26 wherein the distributor comprises a metal sparger diffuser.