Methods for fuel conversion

US10144640B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10144640-B2
Application numberUS-201414766086-A
CountryUS
Kind codeB2
Filing dateFeb 5, 2014
Priority dateFeb 5, 2013
Publication dateDec 4, 2018
Grant dateDec 4, 2018

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.

In one embodiment described herein, fuel may be converted into syngas by a method comprising feeding the fuel and composite metal oxides into a reduction reactor in a co-current flow pattern relative to one another, reducing the composite metal oxides with the fuel to form syngas and reduced composite metal oxides, transporting the reduced composite metal oxides to an oxidation reactor, regenerating the composite metal oxides by oxidizing the reduced composite metal oxides with an oxidizing reactant in the oxidation reactor, and recycling the regenerated composite metal oxides to the reduction reactor for subsequent reduction reactions to produce syngas. The composite metal oxides may be solid particles comprising a primary metal oxide and a secondary metal oxide.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method for converting gaseous fuel into syngas, the method comprising: feeding the gaseous fuel and composite metal oxides into a reduction reactor having a top and a bottom, wherein the gaseous fuel and the composite metal oxides are fed into the top of the reduction reactor, whereupon the composite metal oxides form a packed bed and the composite metal oxides and the gaseous fuel flow downward through the reactor in a co-current flow pattern relative to one another; reducing the composite metal oxides with the gaseous fuel in the reduction reactor to form syngas and reduced composite metal oxides wherein the syngas comprises hydrogen and carbon monoxide; removing the syngas and the reduced composite metal oxides from the bottom of the reduction reactor; transporting the reduced composite metal oxides to an oxidation reactor; regenerating the composite metal oxides by oxidizing the reduced composite metal oxides with an oxidizing reactant in the oxidation reactor; and recycling the regenerated composite metal oxides to the reduction reactor for subsequent reduction reactions to produce syngas in the reduction reactor; wherein the composite metal oxides comprise iron, titanium and oxygen and the reduced metal oxides comprise FeO.TiO 2 , or wherein the composite metal oxides comprise iron aluminum and oxygen and the reduced metal oxides comprise FeO.Al 2 O 3 . 2. The method of claim 1 , wherein the fuel is natural gas. 3. The method of claim 1 , wherein the oxidizing reactant comprises air, oxygen, steam, carbon dioxide, or any combination thereof. 4. The method of claim 1 , wherein a ratio of hydrogen to carbon monoxide can be controlled. 5. The method of claim 1 , wherein the syngas comprises a stoichiometric ratio of carbon monoxide to hydrogen of about 1:2 and the gaseous fuel is natural gas. 6. The method of claim 1 , wherein the gaseous fuel is co-injected with a carbon-rich or hydrogen-rich reactant to change the carbon monoxide to hydrogen ratio of the syngas. 7. The method of claim 1 , wherein oxygen or oxygen releasing material is introduced in the reduction reaction to increase reaction kinetics for syngas production. 8. The method of claim 1 , wherein the reducing of the composite metal oxides occurs at a temperature in the range of between about 500° C. and about 1200° C. 9. The method of claim 1 , wherein the syngas comprises at least about 85 mol % carbon monoxide and hydrogen. 10. The method of claim 1 , wherein the syngas comprises less than about 10 mol % of carbon dioxide and less than about 10 mol % steam. 11. The method of claim 1 , wherein the composite metal oxides further comprises a dopant/promoter comprising Ca, Ce, Pt, Ru, Rh, La, Fe, Cu, oxides thereof, or any combination thereof.

Assignees

Inventors

Classifications

  • moved by gravity in a downward flow · CPC title

  • Natural gas or methane · CPC title

  • Gasification using molten salts or metals (C10J3/02, C10J3/46 take precedence) · CPC title

  • Processes for making hydrogen or synthesis gas · CPC title

  • Biomass · 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 US10144640B2 cover?
In one embodiment described herein, fuel may be converted into syngas by a method comprising feeding the fuel and composite metal oxides into a reduction reactor in a co-current flow pattern relative to one another, reducing the composite metal oxides with the fuel to form syngas and reduced composite metal oxides, transporting the reduced composite metal oxides to an oxidation reactor, regener…
Who is the assignee on this patent?
Ohio State Innovation Foundation
What technology area does this patent fall under?
Primary CPC classification C01B3/344. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Dec 04 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 7 related publications on this page (citations in our corpus or others sharing the same primary CPC).