IP Library Granted Patent US 12686893
Granted Patent B2
US 12686893 · App. 18/799,808 · Granted Jul 21, 2026

Direct reduced iron system and method

Inventors: Brad True (Rock Hill, SC); Lindsay Leveen (Sausalito, CA); Mirmohammadyousef Motamedhashemi (Gonzales, LA)
Assignee: NUCOR CORPORATION
C21B13/0073C01B3/025C01B3/36C01C1/04C10G2/50C10L1/08C01B2203/0255C01B2203/062C01B2203/068C10G2400/08C10L2200/043C10L2270/04C10L2290/42
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Quick Facts
Patent No.
US 12686893
App. No.
18/799,808
Granted
Jul 21, 2026
Kind
B2
Abstract

A method of direct reduction of iron (DRI) is disclosed, the method comprising generating metallic iron by removing oxygen from iron ore using a reducing gaseous mixture with excess carbon monoxide that produces an excess CO 2 by-product is provided. CO 2 by-product is optionally sequestered. A system for carrying out the method is also disclosed.

Claims (16)

1 . A method of direct reduction of iron (DRI) comprising:

reducing a source of iron ore with a reducing gaseous mixture feed to produce a direct reduced iron product and a top gas feed;

scrubbing the top gas feed;

separating the top gas feed to provide a carbon dioxide by-product feed and an unreacted hydrogen and carbon monoxide feed;

processing unreacted hydrogen and/or unreacted carbon monoxide from the unreacted hydrogen and carbon monoxide feed to provide a carbon monoxide feed and an essentially pure hydrogen feed; and

sequestering the carbon dioxide by-product feed;

wherein the reducing gaseous mixture feed is provided to a DRI unit by a partial oxidation unit (POX).

2 . The method of claim 1 , wherein the reducing gaseous mixture feed comprises hydrogen and carbon monoxide.

3 . The method of claim 2 , wherein additional carbon monoxide is added to the reducing gaseous mixture feed.

4 . The method of claim 1 , wherein the CO 2 by-product feed is separated from water vapor and the unreacted reducing gaseous mixture feed prior to sequestering.

5 . The method of claim 1 , wherein the CO 2 by-product feed is dried prior to sequestering.

6 . The method of claim 1 , wherein the CO 2 by-product feed is compressed to a supercritical state prior to sequestering.

7 . The method of claim 1 , wherein unreacted hydrogen from the reducing gaseous mixture feed is separated from water vapor and the unreacted reducing gaseous mixture feed prior to sequestering.

8 . The method of claim 7 , wherein the unreacted hydrogen is captured and stored.

9 . The method of claim 1 , further comprising introducing the direct reduced iron product to an electric arc furnace.

10 . The method of claim 9 , wherein the introducing of the direct reduced iron product to an electric arc furnace is continuous or semi-continuous.