Regeneration of a titanium containing zeolite
US-2016332152-A1 · Nov 17, 2016 · US
US9611198B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9611198-B2 |
| Application number | US-201214113366-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 17, 2012 |
| Priority date | Apr 18, 2011 |
| Publication date | Apr 4, 2017 |
| Grant date | Apr 4, 2017 |
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The various embodiments relate to a system and method for regenerating a direct oxidation catalyst that coverts H 2 S to elemental S. One embodiment of the method comprises regenerating a direct oxidation catalyst by contacting the direct oxidation catalyst with steam.
Opening claim text (preview).
The invention claimed is: 1. A process for treating a gas stream, the process comprising: contacting a gas stream comprising hydrogen sulfide and at least one hydrocarbon component with an oxygen-containing gas in the presence of a direct oxidation catalyst; monitoring the amount of sulfur dioxide generated by contacting the gas stream with the direct oxidation catalyst; and regenerating the direct oxidation catalyst when the amount of sulfur dioxide reaches a predetermined limit by contacting the direct oxidation catalyst with steam to regenerate the direct oxidation catalyst. 2. The process of claim 1 wherein in the step of contacting the direct oxidation catalyst with steam to regenerate the direct oxidation catalyst comprises: contacting the direct oxidation catalyst with mixture comprising steam and oxygen. 3. The process of claim 1 wherein the gas stream is contacted with the oxygen-containing gas in the presence of a direct oxidation catalyst in at least one first reactor. 4. The process of claim 3 wherein the method further comprises: diverting the gas stream to at least one second reactor comprising the direct oxidation catalyst before regenerating the direct oxidation catalyst in the first reactor; and contacting gas stream with the oxygen-containing gas and the direct oxidation catalyst in the second reactor. 5. The process of claim 3 further comprising converting carbonyl sulfide in the gas stream to hydrogen sulfide in at least one first carbonyl sulfide reactor. 6. The process of claim 5 further comprising contacting the gas stream with oxygen in the presence of the direct oxidation catalyst after the gas stream exits the carbonyl sulfide reactor.
Catalyst compositions · CPC title
Recycling of catalysts · CPC title
of catalysts comprising metals, oxides or hydroxides of the noble metals · CPC title
using steam · CPC title
of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper · CPC title
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