Calcium oxide or magnesium oxide production with alkali and sulfur dioxide intermediates
US-12017985-B2 · Jun 25, 2024 · US
US11155462B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11155462-B2 |
| Application number | US-201916505378-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 8, 2019 |
| Priority date | Apr 8, 2019 |
| Publication date | Oct 26, 2021 |
| Grant date | Oct 26, 2021 |
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.
Methods and systems for producing hydrogen substantially without greenhouse gas emissions, the method including producing a product gas comprising hydrogen and carbon dioxide from a hydrocarbon fuel source; separating hydrogen from the product gas to create a hydrogen product stream and a byproduct stream; injecting the byproduct stream into a reservoir containing mafic rock; and allowing components of the byproduct stream to react in situ with components of the mafic rock to precipitate and store components of the byproduct stream in the reservoir.
Opening claim text (preview).
What is claimed is: 1. A method for producing hydrogen substantially without greenhouse gas emissions, the method comprising the steps of: producing a product gas comprising hydrogen and carbon dioxide from a hydrocarbon fuel source; separating hydrogen from the product gas to create a hydrogen product stream and a byproduct stream comprising CO 2 ; disposing the byproduct stream comprising CO 2 in an aqueous phase as a water soluble gas to form a CO 2 -rich water phase with a density greater than ambient groundwater; injecting the byproduct stream into a reservoir containing mafic rock; and allowing components of the byproduct stream to react in situ with components of the mafic rock to precipitate and store components of the byproduct stream in the reservoir. 2. The method according to claim 1 , where the mafic rock comprises basaltic rock. 3. The method according to claim 1 , where before the step of injecting the byproduct stream into the reservoir, the byproduct stream is further treated to separate and purify CO 2 from other components to increase CO 2 concentration of the byproduct stream for injection into the reservoir. 4. The method according to claim 3 , further comprising the step of liquefying CO 2 in the byproduct stream for injection into the reservoir. 5. The method according to claim 1 , where the byproduct stream further comprises H 2 S. 6. The method according to claim 1 , further comprising the step of reacting the separated hydrogen with nitrogen to form compressed liquid ammonia. 7. The method according to claim 6 , further comprising the steps of transporting the compressed liquid ammonia and returning the compressed liquid ammonia to hydrogen and nitrogen via electrolysis for use of hydrogen as a hydrogen fuel source. 8. The method according to claim 1 , where the step of producing a product gas includes steam reforming or partial oxidation. 9. The method according to claim 1 , where the step of allowing components of the byproduct stream to react in situ with components of the mafic rock to precipitate produces precipitates selected from the group consisting of: calcium carbonates, magnesium carbonates, iron carbonates, and combinations thereof. 10. The method according to claim 1 , where the reservoir is between about 250 m and about 2,200 m below the surface and is between about 30° C. and about 325° C. 11. The method according to claim 1 , where the reservoir is between about 350 m and about 1,500 m below the surface and is less than about 325° C. 12. The method according to claim 1 , wherein a ratio of water in the aqueous phase to CO 2 in the byproduct stream comprising CO 2 is about 27 tons of H 2 O per 1 ton of CO 2 .
Carbon dioxide sequestration · CPC title
Natural gas or methane · CPC title
Integration with other chemical processes · CPC title
containing a partial oxidation step · CPC title
the reforming step being a steam reforming step · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.