Zero emissions sulphur recovery process with concurrent hydrogen production

US9981849B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9981849-B2
Application numberUS-201614989696-A
CountryUS
Kind codeB2
Filing dateJan 6, 2016
Priority dateMay 6, 2011
Publication dateMay 29, 2018
Grant dateMay 29, 2018

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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Abstract

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.

First claim

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.

Assignees

Inventors

Classifications

  • 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

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What does patent US9981849B2 cover?
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 comprisin…
Who is the assignee on this patent?
Stamicarbon, Stamicarbon B V Acting Under The Name Of Mt Innovation Center
What technology area does this patent fall under?
Primary CPC classification C01B17/0495. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue May 29 2018 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).