Methods for producing syngas from H2S and CO2 in an electrochemical cell

US12018392B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-12018392-B2
Application numberUS-202217567465-A
CountryUS
Kind codeB2
Filing dateJan 3, 2022
Priority dateJan 3, 2022
Publication dateJun 25, 2024
Grant dateJun 25, 2024

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

The present application provides systems, apparatuses, and methods for simultaneous processing of tow waster gases, namely H2S and CO2. In an exemplary process of this disclosure H2S is supplied to anode side of an electrochemical cell, while CO2 is supplied to the cathode side. As a result, valuable commercial products are produced. In particular, SO2 is harvested from the anode side, while synthesis gas, CO+H2) is harvested from the cathode side. An electric current is also produced, which can be supplied to a local utility grid.

First claim

Opening claim text (preview).

What is claimed is: 1. A method for producing syngas and SO 2 from H 2 S, CO 2 , and H 2 O in an electrochemical cell comprising an anode, a cathode, and a conductive membrane positioned between and in electrochemical contact with the anode and the cathode, the method comprising: contacting the anode of the electrochemical cell with a stream comprising H 2 S and H 2 O to produce a stream comprising SO 2 ; and contacting the cathode of the electrochemical cell with a stream comprising CO 2 and H 2 O to produce a stream comprising syngas. 2. The method of claim 1 , wherein contacting the anode and contacting the cathode occur simultaneously. 3. The method of claim 1 , further comprising collecting the stream comprising SO 2 from the anode side of the electrochemical cell. 4. The method of claim 1 , further comprising collecting the stream comprising the syngas from the cathode side of the electrochemical cell. 5. The method of claim 1 , wherein the stream comprising H 2 S and H 2 O is a gas. 6. The method of claim 5 , wherein the pressure of the stream is from about 1 bar to about 20 bar. 7. The method of claim 5 , wherein the temperature of the stream is from about 100° C. to about 1,500° C. 8. The method of claim 5 , wherein molar ratio of H 2 S to H 2 O in the stream is from about 0.1:1 to about 10:1. 9. The method of claim 5 , wherein temperature of the stream is from about 700° C. to about 1,000° C. 10. The method of claim 1 , wherein the anode material comprises WS 2 , CoS 1.035 or Li 2 S. 11. The method of claim 1 , wherein the stream comprising CO 2 and H 2 O is a gas. 12. The method of claim 11 , wherein the pressure of the stream is from about 1 bar to about 20 bar. 13. The method of claim 11 , wherein the temperature of the stream is from about 100° C. to about 1,500° C. 14. The method of claim 11 , wherein molar ratio of CO 2 to H 2 O in the stream is from about 0.1:1 to about 10:1. 15. The method of claim 11 , wherein temperature of the stream is from about 700° C. to about 1,000° C. 16. The method of claim 1 , wherein the cathode material comprises a perovskite material of the general type La 1-x Sr x Cr 1-y M y O 3 , where M is a metal selected from Mn, Fe, Co, and Ni. 17. The method of claim 1 , wherein the conductive membrane comprises a material selected from yttria-stabilized zirconia (YSZ), scandia stabilized zirconia (ScSZ), gadolinium doped ceria (GDC), lanthanum strontium cobalt ferrite (LSCF), Sr-doped La manganites (LSM), and ferrites-nickelates (LSFN). 18. The method of claim 1 , wherein molar ratio of H 2 S to CO 2 in the electrochemical cell is from about 0.1:1 to about 10:1. 19. The method of claim 1 , wherein molar ratio of CO to H 2 in the syngas is from about 1:1 to about 1:5. 20. The method of claim 1 , wherein the syngas comprises no more than from about 0.5 wt. % to about 10 wt. % of CO 2 or H 2 O, or a combination thereof.

Assignees

Inventors

Classifications

  • in electrochemical cells · CPC title

  • of inorganic oxides or hydroxides · CPC title

  • Sulfides · CPC title

  • by electrochemical means (H01M8/065 takes precedence) · CPC title

  • characterised by membrane-electrode assemblies [MEA] (H01M8/12 takes precedence) · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US12018392B2 cover?
The present application provides systems, apparatuses, and methods for simultaneous processing of tow waster gases, namely H2S and CO2. In an exemplary process of this disclosure H2S is supplied to anode side of an electrochemical cell, while CO2 is supplied to the cathode side. As a result, valuable commercial products are produced. In particular, SO2 is harvested from the anode side, while sy…
Who is the assignee on this patent?
Saudi Arabian Oil Co
What technology area does this patent fall under?
Primary CPC classification C25B5/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jun 25 2024 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 12 related publications on this page (citations in our corpus or others sharing the same primary CPC).