Method for the direct reduction of iron ore
US-2022389528-A1 · Dec 8, 2022 · US
US2024263259A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024263259-A1 |
| Application number | US-202118559901-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 26, 2021 |
| Priority date | May 26, 2021 |
| Publication date | Aug 8, 2024 |
| Grant date | — |
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.
A method of operating a network of plants comprising a blast furnace, a direct reduction furnace, a CO2 conversion unit wherein blast furnace top gas is subjected to a CO2 conversion step to produce a liquid carbon product which is injected into the direct reduction furnace.
Opening claim text (preview).
What is claimed is: 1 - 12 . (canceled) 13 . A method of operating a network of plants comprising: producing hot metal and a blast furnace top gas in a blast furnace; charging oxidized iron to a direct reduction furnace to be reduced by a reducing gas to produce direct reduced iron, the direct reduction furnace comprising a reduction zone, a transition zone and a cooling zone; subjecting the blast furnace top gas to a CO2 conversion step in a CO2 conversion unit to produce a liquid carbon product; and injecting the liquid carbon product into the direct reduction furnace. 14 . The method as recited in claim 13 wherein the liquid carbon product is injected at least into the transition zone of the direct reduction furnace. 15 . The method as recited in claim 13 wherein the liquid carbon product is injected at least into the cooling zone of the direct reduction furnace. 16 . The method as recited in claim 13 wherein the liquid carbon product is injected in the transition zone and in the cooling zone of the direct reduction furnace. 17 . The method as recited in claim 13 wherein the liquid carbon product is a biofuel. 18 . The method as recited in claim 13 wherein the liquid carbon product is liquid alcohol. 19 . The method as recited in claim 13 wherein the liquid carbon product is liquid hydrocarbon. 20 . The method as recited in claim 13 wherein the reducing gas comprises more than 50% in volume of hydrogen. 21 . The method as recited in claim 13 wherein the reducing gas comprises more than 99% in volume of hydrogen. 22 . The method as recited in claim 13 wherein the network of plants further comprises a coke oven producing coke and a coke oven gas, the coke oven gas being mixed with blast furnace gas to be turned into the liquid carbon product. 23 . The method as recited in claim 13 further comprising producing liquid steel and a steelmaking gas in a steelmaking plant, the steelmaking gas being mixed with blast furnace gas to be turned into the liquid carbon product. 24 . The method as recited in claim 13 wherein the CO2 conversion step comprises a biological transformation step.
Selection or treatment of the reducing gases · CPC title
by adding additional fuel in recirculation pipes · CPC title
Interaction of exhaust gases produced during the manufacture of iron or steel with other processes · CPC title
by reforming · CPC title
of carbon dioxide · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.