Processing of sulfur species with deep eutectic solvents or ionic liquids
US-2024399293-A1 · Dec 5, 2024 · US
US9981849B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9981849-B2 |
| Application number | US-201614989696-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 6, 2016 |
| Priority date | May 6, 2011 |
| Publication date | May 29, 2018 |
| Grant date | May 29, 2018 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Disclosed is a process for the concurrent production of hydrogen and sulphur from a H 2 S-containing gas stream, with reduced, and preferably zero, emissions. The method comprises the catalytic oxidative cracking of H 2 S so as to form H 2 and S 2 . Preferably, the oxidation is conducted using oxygen-enriched air, preferably pure oxygen. The process is conducted in a reaction chamber comprising a bifunctional catalyst material, so as to favor both the partial oxidation of H 2 S and the dissociation thereof.
Opening claim text (preview).
The invention claimed is: 1. A plant suitable for conducting catalytic oxidative cracking of an H 2 S-containing gas stream, said plant comprising a catalytic reaction chamber having a first inlet for an H 2 S-containing acid gas stream and a second inlet for an oxygen-comprising stream and comprising a reaction zone containing in series a first catalyst bed filled with a first catalyst for H 2 S partial oxidation and downstream thereof a second catalyst bed filled with a second catalyst for H 2 S cracking; wherein the first catalyst is an oxidation catalyst selected from the group consisting of one or more Group VIII metals and oxides thereof and the second catalyst is a cracking catalyst which is one or more metal sulphides; and wherein the reaction chamber further comprises a gas quench zone downstream from the reaction zone; and wherein said plant further comprises, upstream of said catalytic beds, a static mixer configured for mixing gases from said first and second inlets. 2. A plant according to claim 1 , wherein said gas quench zone comprises a water sprayer. 3. The plant according to claim 1 , wherein the second catalyst is selected from the group consisting of CoS 2 , NiS, NiS 2 , WS 2 , MoS 2 , FeS 2 , Ag 2 S, CuS, CdS, MnS, ZnS, and Cr 2 S 3 . 4. The plant according to claim 1 which further comprises a waste heat boiler and a sulphur condenser downstream of the reaction chamber.
Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title
by dissociation of hydrogen sulfide into the elements · CPC title
by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process · CPC title
Hydrogen · CPC title
Oxygen · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.